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1

Purifying Aluminum by Vacuum Distillation  

NASA Technical Reports Server (NTRS)

Proposed method for purifying aluminum employs one-step vacuum distillation. Raw material for process impure aluminum produced in electrolysis of aluminum ore. Impure metal melted in vacuum. Since aluminum has much higher vapor pressure than other constituents, boils off and condenses on nearby cold surfaces in proportions much greater than those of other constituents.

Du Fresne, E. R.

1985-01-01

2

Application of vacuum membrane distillation for ammonia removal  

Microsoft Academic Search

This study aims to investigate the applicability of membrane distillation for ammonia removal from its aqueous solutions. Among the different recognized membrane distillation configurations, vacuum membrane distillation is applied in the present work for ammonia removal. The effects of different operating parameters on ammonia removal from aqueous solutions of different concentrations have been investigated. Experimental results showed that high feed

M. S. EL-Bourawi; M. Khayet; R. Ma; Z. Ding; Z. Li; X. Zhang

2007-01-01

3

EVALUATION OF A VACUUM DISTILLER FOR PERFORMING METHOD 8261 ANALYSES  

EPA Science Inventory

Vacuum distillation uses a specialized apparatus. This apparatus has been developed and patented by the EPA. Through the Federal Technology Transfer Act this invention has been made available for commercialization. Available vendors for this instrumentation are being evaluated. ...

4

A Hydration of an Alkyne Illustrating Steam and Vacuum Distillation.  

ERIC Educational Resources Information Center

Reports on the conversion 2,5-dimethylhexyne-2,5-diol(I) to 2,2,5,5-tetramethyltetrahydrofuran-3-one(II) using aqueous mercuric sulfate without the use of acid. The experiment has been successfully performed in introductory organic chemistry laboratories demonstrating alkyne hydration, steam distillation, vacuum distillation, drying of organic…

Wasacz, J. P.; Badding, V. G.

1982-01-01

5

Solar power water distillation unit  

NASA Astrophysics Data System (ADS)

Clean drinking water is the basic necessity for every human being, but about 1.1 billion people in the world lacked proper drinking water. There are many different types of water purification processes such as filtration, reverse osmosis, ultraviolet radiation, carbon absorption, but the most reliable processes are distillation and boiling. Water purification, such as distillation, is especially important in regions where water resources or tap water is not suitable for ingesting without boiling or chemical treatment. In design project It treats the water by combining different methods such as Filtration, Distillation and a technique called concentrated solar power (CSP). Distillation is literally the method seen in nature, whereby: the sun heats the water on the earth's surface, the water is turned into a vapor (evaporation) and rises, leaving contaminants behind, to form clouds. As the upper atmosphere drops in temperature the vapors cool and convert back to water to form water. In this project distillation is achieved by using a parabolic mirror which boils water at high temperature. Filtration is done by sand filter and carbon filter. First sand filter catches the sand particles and the carbon filter which has granules of active carbon is used to remove odor dissolved gases from water. This is the Pre-treatment of water. The filtered water is then collected in a water container at a focus of parabolic mirror where distillation process is done. Another important feature of designed project is the solar tracking of a parabolic mirror which increases the efficiency of a parabolic mirror [1],[2].

Hameed, Kamran; Muzammil Khan, Muhammad; Shahrukh Ateeq, Ijlal; Omair, Syed Muhammad; Ahmer, Muhammad; Wajid, Abdul

2013-06-01

6

Vacuum distillation residue upgrading by an indigenous bacillus cereus  

PubMed Central

Background Biological processing of heavy fractions of crude oils offers less severe process conditions and higher selectivity for refining. Biochemical Processes are expected to be low demand energy processes and certainly ecofriendly. Results A strain of biosurfactant producing bacterium was isolated from an oil contaminated soil at Tehran refinery distillation unit. Based on selected phenotypic and genotypic characteristic including morphology, biochemical proprety, and 16 SrRNA sequencing identified as a novel strain of Bacillus cereus (JQ178332). This bacterium endures a wide range of pH, salinity and temperature. This specific strain utilizes both paraffin and anthracene as samples of aliphatic and polycyclic aromatic hydrocarbons. The ability of this bacterium to acquire all its energy and chemical requirements from Vacuum Distillation Residue (VR), as a net sample of problematic hydrocarbons in refineries, was studied. SARA test ASTM D4124-01 revealed 65.5% decrease in asphaltenic, 22.1% in aliphatics and 30.3% in Aromatics content of the VR in MSM medium. Further results with 0.9% saline showed 55% decrease in asphaltene content and 2.1% Aromatics respectively. Conclusion Remarkable abilities of this microorganism propose its application in an ecofriendly technology to upgrade heavy crude oils. PMID:24499629

2013-01-01

7

VOLATILE ORGANO-METALLOIDS IN BIO-SOLID MATERIALS: ANALYSIS BY VACUUM DISTILLATION-GC/MS  

EPA Science Inventory

An analytical method based on vacuum distillation-gas chromatography-mass spectrometry (VD-GC-MS) was developed for determining volatile organo-metalloid contaminants in bio-solid materials. Method performance was evaluated for dimethylselenide (DMSe), dimethyldisel...

8

Vacuum distillation: vapor filtered-catalytic oxidation water reclamation system utilizing radioisotopes  

NASA Technical Reports Server (NTRS)

The development of a functional model water reclamation system is discussed. The system produces potable water by distillation from the urine and respiration-perspiration condensate at the normal rate generated by four men. Basic processes employed are vacuum distillation, vapor filtration, vapor phase catalytic oxidation, and condensation. The system is designed to use four 75-watt isotope heaters for distillation thermal input, and one 45-watt isotope for the catalytic oxidation unit. The system is capable of collecting and storing urine, and provides for stabilizing the urine by chemical pretreatment. The functional model system is designed for operation in a weightless condition with liquid-vapor phase separators for the evaporator still, and centrifugal separators for urine collection and vapor condensation. The system provides for storing and dispensing reclaimed potable water. The system operates in a batch mode for 40 days, with urine residues accumulating in the evaporator. The evaporator still and residue are removed to storage and replaced with a fresh still for the next 40-day period.

Honegger, R. J.; Remus, G. A.; Kurg, E. K.

1971-01-01

9

PILOT-SCALE REMOVAL OF FLUORIDE FROM LEGACY PLUTONIUM MATERIALS USING VACUUM SALT DISTILLATION  

SciTech Connect

Between September 2009 and January 2011, the Savannah River National Laboratory (SRNL) and HB-Line designed, developed, tested, and successfully deployed a system for the distillation of chloride salts. In 2011, SRNL adapted the technology for the removal of fluoride from fluoride-bearing salts. The method involved an in situ reaction between potassium hydroxide (KOH) and the fluoride salt to yield potassium fluoride (KF) and the corresponding oxide. The KF and excess KOH can be distilled below 1000{deg}C using vacuum salt distillation (VSD). The apparatus for vacuum distillation contains a zone heated by a furnace and a zone actively cooled using either recirculated water or compressed air. During a vacuum distillation operation, a sample boat containing the feed material is placed into the apparatus while it is cool, and the system is sealed. The system is evacuated using a vacuum pump. Once a sufficient vacuum is attaned, heating begins. Volatile salts distill from the heated zone to the cooled zone where they condense, leaving behind the non-volatile material in the feed boat. Studies discussed in this report were performed involving the use of non-radioactive simulants in small-scale and pilot-scale systems as well as radioactive testing of a small-scale system with plutonium-bearing materials. Aspects of interest include removable liner design considerations, boat materials, in-line moisture absorption, and salt deposition.

Pierce, R. A.; Pak, D. J.

2012-09-11

10

Vacuum distillation/vapor filtration water recovery, phases 1 and 2  

NASA Technical Reports Server (NTRS)

The research is reported on the development of an evaporator for vacuum distillation/vapor filtration VD/VF water reclamation system for use on manned space flights. The design, fabrication, and tests of a six-man evaporator are described. It is concluded that: (1) A condenser with an internal rotating impeller and coolant surfaces directly opposite the condensing surfaces is an effective condenser. (2) The VD/VF evaporator, catalyst unit and condenser function satisfactorily based on thermal, mechanical and recovery performance during a 145-hour evaluation test. (3) The quality of recovered water, as measured by analyses for total organic carbon, pH, conductivity, turbidity, and viable bacteria density was within established limits for potability.

Honegger, R. J.; Remus, G. A.; Krug, E. K.

1973-01-01

11

Geothermal Energy Market Study on the Atlantic Coastal Plain: Technical Feasibility of use of Eastern Geothermal Energy in Vacuum Distillation of Ethanol Fuel  

SciTech Connect

The DOE is studying availability, economics, and uses of geothermal energy. These studies are being conducted to assure maximum cost-effective use of geothermal resources. The DOE is also aiding development of a viable ethanol fuel industry. One important point of the ethanol program is to encourage use of non-fossil fuels, such as geothermal energy, as process heat to manufacture ethanol. Geothermal waters available in the eastern US tend to be lower in temperature (180 F or less) than those available in the western states (above 250 F). Technically feasible use of eastern geothermal energy for ethanol process heat requires use of technology that lowers ethanol process temperature requirements. Vacuum (subatmospheric) distillation is one such technology. This study, then, addresses technical feasibility of use of geothermal energy to provide process heat to ethanol distillation units operated at vacuum pressures. They conducted this study by performing energy balances on conventional and vacuum ethanol processes of ten million gallons per year size. Energy and temperature requirements for these processes were obtained from the literature or were estimated (for process units or technologies not covered in available literature). Data on available temperature and energy of eastern geothermal resources was obtained from the literature. These data were compared to ethanol process requirements, assuming a 150 F geothermal resource temperature. Conventional ethanol processes require temperatures of 221 F for mash cooking to 240 F for stripping. Fermentation, conducted at 90 F, is exothermic and requires no process heat. All temperature requirements except those for fermentation exceed assumed geothermal temperatures of 150 F. They assumed a 130 millimeter distillation pressure for the vacuum process. It requires temperatures of 221 F for mash cooking and 140 F for distillation. Data indicate lower energy requirements for the vacuum ethanol process (30 million BTUs per hour) than for the conventional process (36 million BTUs per hour). Lower energy requirements result from improved process energy recovery. Data examined in this study indicate feasible use of eastern geothermal heated waters (150 F) to provide process heat for vacuum (130 mm Hg) ethanol distillation units. Data indicate additional heat sources are needed to raise geothermal temperatures to the 200 F level required by mash cooking. Data also indicate potential savings in overall process energy use through use of vacuum distillation technology. Further study is needed to confirm conclusions reached during this study. Additional work includes obtaining energy use data from vacuum ethanol distillation units currently operating in the 130 millimeter pressure range; economic analysis of different vacuum pressures to select an optimum; and operation of a pilot geothermally heated vacuum column to produce confirmatory process data.

None

1981-04-01

12

Coal liquefaction using vacuum distillation and an external residuum feed  

SciTech Connect

A process for liquefying coal in which a slurry comprising a petroleum or petroleum-derived solvent and particulate coal is heated in a dissolution zone to substantially dissolve the coal and produce a first effluent containing undissolved solids to which petroleum residuum is added to produce a second effluent which is distilled under reduced pressure. The process eliminates the need for physical solids separation such as filtration or centrifugation and is most advantageously employed in high-severity coal liquefaction.

Kuehler, C.W.

1985-04-09

13

Changes in14c activity over time during vacuum distillation of carbon from rock pore water  

USGS Publications Warehouse

The radiocarbon activity of carbon collected by vacuum distillation from a single partially saturated tuff began to decline after approximately 60% of the water and carbon had been extracted. Disproportionate changes in 14C activity and ??13C during distillation rule out simple isotopic fractionation as a causative explanation. Additional phenomena such as matrix diffusion and ion exclusion in micropores may play a role in altering the isotopic value of extracted carbon, but neither can fully account for the observed changes. The most plausible explanation is that distillation recovers carbon from an adsorbed phase that is depleted in 14C relative to DIC in the bulk pore water. ?? 1999 by the Arizona Board of Regents on behalf of the University of Arizona.

Davidson, G.R.; Yang, I.C.

1999-01-01

14

High vacuum distillation of ionic liquids and separation of ionic liquid mixtures.  

PubMed

The vaporisation of ionic liquids has been investigated using temperature programmed desorption (TPD) and ultra-high vacuum (UHV) distillation. 1-Alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquids, [C(n)C(1)Im][Tf(2)N] (n = 2, 8), have been distilled at UHV and T > 500 K in a specially designed still. The distillation process yielded spectroscopically pure ionic liquid distillates with complete removal of volatile impurities such as water, argon and 1-methylimidazole. Such UHV distillation offers a method of obtaining high purity ionic liquids for analytical applications. The vapour phase of the ionic liquid mixtures [C(2)C(1)Im](0.05)[C(8)C(1)Im](0.95)[Tf(2)N] and [C(2)C(1)Im][C(8)C(1)Im][Tf(2)N][EtSO(4)] has been analysed by TPD using line-of-sight mass spectrometry (LOSMS). The vapour phase consisted of all possible combinations of neutral ion pairs (NIPs) from the liquid mixture. Neither mixture showed evidence of decomposition during TPD, and the [C(2)C(1)Im](0.05)[C(8)C(1)Im](0.95)[Tf(2)N] mixture was shown to obey Raoult's law. Based on the TPD results, fractional distillations were attempted for [C(2)C(1)Im][C(8)C(1)Im][Tf(2)N](2) and [C(2)C(1)Im][C(8)C(1)Im][Tf(2)N][EtSO(4)] mixtures. The distillate from [C(2)C(1)Im][C(8)C(1)Im][Tf(2)N](2) was enhanced in the more volatile [C(2)C(1)Im][Tf(2)N] components, but the [C(2)C(1)Im][C(8)C(1)Im][Tf(2)N][EtSO(4)] mixture underwent significant decomposition. The similarities and differences between UHV TPD, and high vacuum distillation, of ionic liquids, are discussed. Design parameters are outlined for a high vacuum ionic liquid still that will minimise decomposition and maximise separation of ILs of differing volatility. PMID:20145842

Taylor, Alasdair W; Lovelock, Kevin R J; Deyko, Alexey; Licence, Peter; Jones, Robert G

2010-02-28

15

Hydrothermal liquefaction of microalgae for biocrude production: Improving the biocrude properties with vacuum distillation.  

PubMed

This paper proposes a two-part process for producing biocrude with reduced impurities. The biocrude was produced from hydrothermal liquefaction (HTL) of Spirulina sp. and Tetraselmis sp. in a batch reactor at both 300 and 350°C, 5min, and 16%w/w solid feed composition. The resultant biocrudes were vacuum distilled at a maximum temperature of 360°C. It was shown that biocrude quality could be enhanced without using catalyst by vacuum distillation (VD). The biocrude yield for Spirulina sp. was 36wt% at 300°C, 42wt% at 350°C, and for Tetraselmis sp. was 34wt% at 300°C, and 58wt% at 350°C. VD of Spirulina sp. biocrude obtained at 300 and 350°C led to 62 and 67wt% distilled biocrudes yield, respectively. VD of Tetraselmis sp. biocrude obtained at 300°C was 70wt%, and 73wt% at 350°C. The higher heating values (HHV) increased from 32MJ/kg to 40MJ/kg. There were substantial reductions in oxygen, metallic content, and boiling point ranges in distilled biocrudes. PMID:25463802

Eboibi, Blessing Elo-Oghene; Lewis, David Milton; Ashman, Peter John; Chinnasamy, Senthil

2014-12-01

16

Distillation  

NSDL National Science Digital Library

Science in its earliest beginnings consisted of a practice called alchemy. Alchemy includes the study of chemistry, biology, astronomy, spirituality, physics, and art. Distillation or experiments in purification of substances may have been a part of the practice of alchemy.

N/A N/A (None;)

2005-12-24

17

Attractancy to Oryzaephilus surinamensis (L.) of volatile materials isolated from vacuum distillate of heat-treated carobs  

Microsoft Academic Search

Vacuum distillation of heat-treated carobs gave an aqueous, colorless, sweet-smelling distillate which was tested over a wide range of concentrations and found to be highly attractive to adultOryzaephilus surinamensis (L.). The materials responsible for the aroma were isolated from the distillate by saturating with sodium chloride and extracting into diethyl ether as separate acidic, neutral, and basic fractions. The extraction

M. R. Stubbs; J. Chambers; S. B. Schofield; J. P. G. Wilkins

1985-01-01

18

Application of MIVM for Sn-Zn System in Vacuum Distillation  

NASA Astrophysics Data System (ADS)

The activities of components of Sn-Zn system were predicted based on the molecular interaction volume model (MIVM). The separation coefficients and the vapor-liquid phase equilibrium of Sn-Zn system were also predicted using the MIVM. The predicted results indicated that the content of tin in the vapor phase was 0.000052 wt pct, while in the liquid phase, it was 99.98 wt pct at 1173 K (900 °C). Experimental investigations into the separation of Sn-Zn alloy by vacuum distillation were carried out for the proper interpretation of the predicted results. The effects of vacuum level (15 to 200 Pa), distillation temperatures [873 K to 1273 K (600 °C to 1000 °C)], and soaking time (20 to 60 minutes) were studied. The experimental results indicated that the content of tin in the vapor phase was 0.001 wt pct, while in the liquid phase, it was 99.98 wt pct at 1173 K (900 °C). The experimental results match well with the predicted data, suggesting that the MIVM is a suitable model for Sn-Zn system.

Kong, LingXin; Yang, Bin; Xu, BaoQiang; Li, YiFu; Hu, Yuanshou; Liu, DaChun

2014-12-01

19

APPLICATION OF VACUUM SALT DISTILLATION TECHNOLOGY FOR THE REMOVAL OF FLUORIDE AND CHLORIDE FROM LEGACY FISSILE MATERIALS  

SciTech Connect

Between September 2009 and January 2011, the Savannah River National Laboratory (SRNL) and the Savannah River Site (SRS) HB-Line Facility designed, developed, tested, and successfully deployed a production-scale system for the distillation of sodium chloride (NaCl) and potassium chloride (KCl) from plutonium oxide (PuO{sub 2}). Subsequent efforts adapted the vacuum salt distillation (VSD) technology for the removal of chloride and fluoride from less-volatile halide salts at the same process temperature and vacuum. Calcium chloride (CaCl{sub 2}), calcium fluoride (CaF{sub 2}), and plutonium fluoride (PuF{sub 3}) were of particular concern. To enable the use of the same operating conditions for the distillation process, SRNL employed in situ exchange reactions to convert the less-volatile halide salts to compounds that facilitated the distillation of halide without removal of plutonium. SRNL demonstrated the removal of halide from CaCl{sub 2}, CaF{sub 2} and PuF{sub 3} below 1000 C using VSD technology.

Pierce, R.; Peters, T.

2011-11-01

20

Apollo telescope mount thermal systems unit thermal vacuum test  

NASA Technical Reports Server (NTRS)

The Apollo Telescope Mount's thermal systems unit was utilized to conduct a full-scale thermal vacuum test to verify the thermal design and the analytical techniques used to develop the thermal mathematical models. Thermal vacuum test philosophy, test objectives configuration, test monitoring, environment simulation, vehicle test performance, and data correlation are discussed. Emphasis is placed on planning and execution of the thermal vacuum test with particular attention on problems encountered in conducting a test of this maguitude.

Trucks, H. F.; Hueter, U.; Wise, J. H.; Bachtel, F. D.

1971-01-01

21

32. VIEW LOOKING WEST SHOWING UNIT #3. VACUUM PUMP ON ...  

Library of Congress Historic Buildings Survey, Historic Engineering Record, Historic Landscapes Survey

32. VIEW LOOKING WEST SHOWING UNIT #3. VACUUM PUMP ON LEFT, CONDENSER TURBINE ON RIGHT, JET CONDENSER IN CENTER REAR - Georgetown Steam Plant, South Warsaw Street, King County Airport, Seattle, King County, WA

22

HYDROGEN DISTILLATION AT THE DEUTERIUM REMOVAL UNIT OF MuCap EXPERIMENT  

E-print Network

321 HYDROGEN DISTILLATION AT THE DEUTERIUM REMOVAL UNIT OF MuCap EXPERIMENT I.A. Alekseev, E hydrogen gas (so- called protium) must be used. It is necessary to avoid transfers of - to impurities imposes strict and critical requirements on the hydrogen gas system supporting the detector. Desirable

Titov, Anatoly

23

Removing lead from metallic mixture of waste printed circuit boards by vacuum distillation: factorial design and removal mechanism.  

PubMed

The lead removal from the metallic mixture of waste printed circuit boards by vacuum distillation was optimized using experimental design, and a mathematical model was established to elucidate the removal mechanism. The variables studied in lead evaporation consisted of the chamber pressure, heating temperature, heating time, particle size and initial mass. The low-level chamber pressure was fixed at 0.1 Pa as the operation pressure. The application of two-level factorial design generated a first-order polynomial that agreed well with the data for evaporation efficiency of lead. The heating temperature and heating time exhibited significant effects on the efficiency, which was validated by means of the copper-lead mixture experiments. The optimized operating conditions within the region studied were the chamber pressure of 0.1 Pa, heating temperature of 1023 K and heating time of 120 min. After the conditions were employed to remove lead from the metallic mixture of waste printed circuit boards, the efficiency was 99.97%. The mechanism of the effects was elucidated by mathematical modeling that deals with evaporation, mass transfer and condensation, and can be applied to a wider range of metal removal by vacuum distillation. PMID:23830119

Li, Xingang; Gao, Yujie; Ding, Hui

2013-10-01

24

A comparison of the toluene distillation and vacuum/heat methods for extracting soil water for stable isotopic analysis  

NASA Astrophysics Data System (ADS)

Hanford Loam, from Richland, Washington, was used as a test soil to determine the precision, accuracy and nature of two methods to extract soil water for stable isotopic analysis: azeotropic distillation using toluene, and simple heating under vacuum. The soil was oven dried, rehydrated with water of known stable isotopic compositions, and the introduced water was then extracted. Compared with the introduced water, initial aliquots of evolved water taken during a toluene extraction were as much as 30 ‰ more depleted in D and 2.7 ‰ more depleted in 18O, whereas final aliquots were as much as 40 ‰ more enriched in D and 14.3 ‰ more enriched in 18O. Initial aliquots collected during the vacuum/heat extraction were as much as 64 ‰ more depleted in D and 8.4 ‰ more depleted in 18O than was the introduced water, whereas the final aliquots were as much as 139 ‰ more enriched in D, and 20.8 ‰ more enriched in 18O. Neither method appears quantitative; however, the difference in stable isotopic composition between the first and last aliquots of water extracted by the toluene method is less than that from the vacuum/heat method. This is attributed to the smaller fractionation factors involved with the higher average temperatures of distillation of the toluene. The average stable isotopic compositions of the extracted water varied from that of the introduced water by up to 1.4 ‰ in ?D and 4.2 ‰ in ?18O with the toluene method, and by 11.0 ‰ in ?D and 1.8 ‰ in ?18O for the vacuum/heat method. The lack of accuracy of the extraction methods is thought to be due to isotopic fractionation associated with water being weakly bound (not released below 110°C) in the soil. The isotopic effect of this heat-labile water is larger at low water contents (3.6 and 5.2% water by weight) as the water bound in the soil is a commensurately larger fraction of the total. With larger soilwater contents the small volume of water bound with an associated fractionation is not enough to affect the remaining unbound introduced soil water. Pretreatment of the soil to equilibrate the heat-labile water to the test water produced good results for the toluene distillation but not the vacuum/heat extraction method. Vapors collected over the soils also show stable isotopic variations related to soilwater content. These vapors also appear to be in closer equilibrium with the free water, as extracted by the toluene method, than with the originally introduced water; thus, the soil vapors do not appear to be isotopically affected by the heat-labile water. The toluene method appears to be better for extracting soil water for stable isotopic analysis because it allows more precise temperature control and excludes the extraction of heat-labile water which is isotopically fractionated. The bound nature of this heat-labile water limits association with the hydrologically active soil water; thus, the exclusion of this water from the soil water attained by toluene distillation may be advantageous. However, the azeotropic nature of toluene distillation affords no benefit and the extraction procedure must continue to completion.

Ingraham, Neil L.; Shadel, Craig

1992-12-01

25

Modeling of crude oil fouling in preheat exchangers of refinery distillation units  

Microsoft Academic Search

The aim of this paper is to propose a new model for crude oil fouling in preheat exchangers of crude distillation units. The experimental results of Australian light crude oil with the tube side surface temperature between 200 and 260°C and fluid velocity ranged 0.25–0.4m\\/s were used [Z. Saleh, R. Sheikholeslami, A.P. Watkinson, Heat exchanger fouling by a light australian

Mohammad Reza Jafari Nasr; Mehdi Majidi Givi

2006-01-01

26

Energy Savings Accomplished by Replacing Steam Ejectors with Electric Driven Vacuum Pumps in Crude Distillation Vacuum Towers  

E-print Network

of the this stationary cone ratio of the pump. inlet and discharae p~rts on determines the compre~sion o IN THIS SECTOR, LIQUID MOYES e IN THIS SECTOR. LIQUID MOVES DurWARD-DRAWS GAS FROM INWARD_COMPRESSESOAS INLET PORTS INTO ROTOR IN ROTOR CHAMBERS CHAMBERS... INLET POll, ROTATING LIQUID COMPRf.SSANT VACLNIM TOWER _ _+-+----.;I--L.c::::-------,-TO LOW ....IUM NOTweU aHIG ACCU.....ATOft OL TO ILOP FlO. 2 PROCESS FLOW HYIIRID VACUUM SYSTEM OATHEMIG LIME Figure 2 shows the process flow...

Nelson, R. E.

1982-01-01

27

Application of Molecular Interaction Volume Model for Phase Equilibrium of Sn-Based Binary System in Vacuum Distillation  

NASA Astrophysics Data System (ADS)

Based on the molecular interaction volume model (MIVM), the activities of components of Sn-Sb, Sb-Bi, Sn-Zn, Sn-Cu, and Sn-Ag alloys were predicted. The predicted values are in good agreement with the experimental data, which indicate that the MIVM is of better stability and reliability due to its good physical basis. A significant advantage of the MIVM lies in its ability to predict the thermodynamic properties of liquid alloys using only two parameters. The phase equilibria of Sn-Sb and Sn-Bi alloys were calculated based on the properties of pure components and the activity coefficients, which indicates that Sn-Sb and Sn-Bi alloys can be separated thoroughly by vacuum distillation. This study extends previous investigations and provides an effective and convenient model on which to base refining simulations for Sn-based alloys.

Kong, Lingxin; Yang, Bin; Xu, Baoqiang; Li, Yifu

2014-09-01

28

Ultrasound-assisted extraction coupled with under vacuum distillation of flavour compounds from spearmint (carvone-rich) plants: Comparison with conventional hydrodistillation.  

PubMed

Ultrasonically assisted extraction of flavour compounds from different varieties of Mentha spicata, using 70% ethanol, have been carried out for 5, 10 and 15min and coupled with under vacuum distillation. The ultrasound distilled extracts have been analysed by GC-MS and compared with essential oils obtained by hydrodistillation. The results have showed that ultrasonically assisted extraction in combination with under vacuum distillation have provided extracts with higher flavouring strength due to the increased concentration of desirable oxygenated compounds (from 5 to 8 times) compared with hydrodistillation. Extraction yields of flavour volatiles have been calculated giving a range 0.04-0.13% by ultrasound and 0.01-0.02% by hydrodistillation. PMID:19406680

Da Porto, Carla; Decorti, Deborha

2009-08-01

29

Fractionation of citronella ( Cymbopogon winterianus) essential oil and concentrated orange oil phase by batch vacuum distillation  

Microsoft Academic Search

The aim of this work was to assess the performance of a vacuum fractionating column for the fractionation of citronella essential oil and concentrated orange oil phase during batch mode operation at different pressures, from 20 to 1mbar and reflux ratios from 1:1 to 10:1. Fractions from column top and bottom were analyzed by gas chromatography (GC\\/FID) using authentic standards

Stephani C. Beneti; Eline Rosset; Marcos L. Corazza; Caren D. Frizzo; Marco Di Luccio; J. Vladimir Oliveira

2011-01-01

30

New Smelting Process for Titanium: Magnesiothermic Reduction of TiCl4 into Liquid Bi and Subsequent Refining by Vacuum Distillation  

NASA Astrophysics Data System (ADS)

We demonstrate a new continuous smelting process for Ti that combines magnesiothermic reduction of TiCl4 into liquid Bi and refining by vacuum distillation. TiCl4 is reduced by Mg into liquid Bi to form Bi-Ti liquid alloys, and subsequently refined by vacuum distillation. The Bi-Ti liquid alloys can be easily transferred from a reduction vessel to a refining vessel; consequently, the reduction and refining steps can be performed continuously. Bi-Ti alloys with various compositions were confirmed to form, and the compositions were controllable via adjustment of the nominal composition of TiCl4, Mg, and Bi. After reduction, the alloys were efficiently separated from MgCl2 by differences in their densities. In addition, vacuum distillation of the alloys purified Ti to be greater than 99.6 at pct. Moreover, consideration of the heat balance in the reduction step indicated that the proposed process has the potential to unlimitedly improve the feed rate of TiCl4 when the concentration of Ti in the alloy is 6 to 7 at pct.

Kado, Yuya; Kishimoto, Akihiro; Uda, Tetsuya

2014-08-01

31

New Smelting Process for Titanium: Magnesiothermic Reduction of TiCl4 into Liquid Bi and Subsequent Refining by Vacuum Distillation  

NASA Astrophysics Data System (ADS)

We demonstrate a new continuous smelting process for Ti that combines magnesiothermic reduction of TiCl4 into liquid Bi and refining by vacuum distillation. TiCl4 is reduced by Mg into liquid Bi to form Bi-Ti liquid alloys, and subsequently refined by vacuum distillation. The Bi-Ti liquid alloys can be easily transferred from a reduction vessel to a refining vessel; consequently, the reduction and refining steps can be performed continuously. Bi-Ti alloys with various compositions were confirmed to form, and the compositions were controllable via adjustment of the nominal composition of TiCl4, Mg, and Bi. After reduction, the alloys were efficiently separated from MgCl2 by differences in their densities. In addition, vacuum distillation of the alloys purified Ti to be greater than 99.6 at pct. Moreover, consideration of the heat balance in the reduction step indicated that the proposed process has the potential to unlimitedly improve the feed rate of TiCl4 when the concentration of Ti in the alloy is 6 to 7 at pct.

Kado, Yuya; Kishimoto, Akihiro; Uda, Tetsuya

2015-02-01

32

Use of solid-phase extraction, reverse osmosis and vacuum distillation for recovery of aromatic sulfonic acids from aquatic environment followed by their determination using liquid chromatography-electrospray ionization tandem mass spectrometry  

Microsoft Academic Search

Three different sample preparation techniques (i) solid-phase extraction, (ii) reverse osmosis and (iii) vacuum distillation have been investigated and the recoveries were compared for determination of highly water-soluble benzene and stilbene sulfonic acids in aqueous environment by liquid chromatography with photodiode array (PDA) and electrospray ionization tandem mass spectrometry (LC–ESI-MS\\/MS). The recoveries were quite high using vacuum distillation (>90%) compared

R. Nageswara Rao; N. Venkateswarlu; Sara Khalid; R. Narsimha; S. Sridhar

2006-01-01

33

Simulation, exergy analysis and application of diabatic distillation to a tertiary amyl methyl ether production unit of a crude oil refinery  

Microsoft Academic Search

This paper presents the results of a detailed exergy analysis of a tertiary amyl methyl ether (TAME) unit of a crude oil refinery and the application of diabatic distillation to the depentanizer tower of the unit. Diabatic distillation is a separation process in which heat is not only supplied to the reboiler and extracted from the condenser [as in a

R. Rivero; M. Garcia; J. Urquiza

2004-01-01

34

Water reclamation from shale gas drilling flow-back fluid using a novel forward osmosis-vacuum membrane distillation hybrid system.  

PubMed

This study examined the performance of a novel hybrid system of forward osmosis (FO) combined with vacuum membrane distillation (VMD) for reclaiming water from shale gas drilling flow-back fluid (SGDF). In the hybrid FO-VMD system, water permeated through the FO membrane into a draw solution reservoir, and the VMD process was used for draw solute recovery and clean water production. Using a SGDF sample obtained from a drilling site in China, the hybrid system could achieve almost 90% water recovery. Quality of the reclaimed water was comparable to that of bottled water. In the hybrid FO-VMD system, FO functions as a pre-treatment step to remove most contaminants and constituents that may foul or scale the membrane distillation (MD) membrane, whereas MD produces high quality water. It is envisioned that the FO-VMD system can recover high quality water not only from SGDF but also other wastewaters with high salinity and complex compositions. PMID:24622553

Li, Xue-Mei; Zhao, Baolong; Wang, Zhouwei; Xie, Ming; Song, Jianfeng; Nghiem, Long D; He, Tao; Yang, Chi; Li, Chunxia; Chen, Gang

2014-01-01

35

High Reliability R-10 Windows Using Vacuum Insulating Glass Units  

SciTech Connect

The objective of this effort was for EverSealed Windows (“EverSealed” or “ESW”) to design, assemble, thermally and environmentally test and demonstrate a Vacuum Insulating Glass Unit (“VIGU” or “VIG”) that would enable a whole window to meet or exceed the an R-10 insulating value (U-factor ? 0.1). To produce a VIGU that could withstand any North American environment, ESW believed it needed to design, produce and use a flexible edge seal system. This is because a rigid edge seal, used by all other know VIG producers and developers, limits the size and/or thermal environment of the VIG to where the unit is not practical for typical IG sizes and cannot withstand severe outdoor environments. The rigid-sealed VIG’s use would be limited to mild climates where it would not have a reasonable economic payback when compared to traditional double-pane or triple-pane IGs. ESW’s goals, in addition to achieving a sufficiently high R-value to enable a whole window to achieve R-10, included creating a VIG design that could be produced for a cost equal to or lower than a traditional triple-pane IG (low-e, argon filled). ESW achieved these goals. EverSealed produced, tested and demonstrated a flexible edge-seal VIG that had an R-13 insulating value and the edge-seal system durability to operate reliably for at least 40 years in the harshest climates of North America.

Stark, David

2012-08-16

36

Vacuum distillation of a mixture of LiCl-KCl eutectic salts and RE oxidative precipitates and a dechlorination and oxidation of RE oxychlorides.  

PubMed

In this study, a vacuum distillation of a mixture of LiCl-KCl eutectic salt and rare-earth oxidative precipitates was performed to separate a pure LiCl-KCl eutectic salt from the mixture. Also, a dechlorination and oxidation of the rare-earth oxychlorides was carried out to stabilize a final waste form. The mixture was distilled under a range of 710-759.5Torr of a reduced pressure at a fixed heating rate of 4 degrees C/min and the LiCl-KCl eutectic salt was completely separated from the mixture. The required time for the salt distillation and the starting temperature for the salt vaporization were lowered with a reduction in the pressure. Dechlorination and oxidation of the rare-earth oxychlorides was completed at a temperature below 1300 degrees C and this was dependent on the partial pressure of O2. The rare-earth oxychlorides (NdOCl/PrOCl) were transformed to oxides (Nd2O3/PrO2) during the dechlorination and oxidation process. These results will be utilized to design a concept for a process for recycling the waste salt from an electrorefining process. PMID:18440139

Eun, Hee Chul; Yang, Hee Chul; Cho, Yung Zun; Lee, Han Soo; Kim, In Tae

2008-12-30

37

Solvent refined coal (SRC) process. Flashing of SRC-II slurry in the vacuum column on Process Development Unit P-99. Interim report, February-June 1980  

SciTech Connect

This report presents the results of 73 tests on the vacuum flash system of Process Development Unit P-99 performed during processing of three different coals; the second batch, fourth shipment (low ash batch) of Powhatan No. 5 Mine (LR-27383), Powhatan No. 6 Mine (LR-27596) and Ireland Mine (LR-27987). The objective of this work was to obtain experimental data for use in confirming and improving the design of the vacuum distillation column for the 6000 ton/day SRC-II Demonstration Plant. The 900/sup 0/F distillate content of the bottoms and the percent of feed flashed overhead were correlated with flash zone operating conditions for each coal, and the observed differences in performance were attributed to differences in the feed compositions. Retrogressive reactions appeared to be occurring in the 900/sup 0/F+ pyridine soluble material leading to an increase in the quantity of pyridine insoluble organic matter. Stream physical properties determined include specific gravity, viscosity and melting point. Elemental, distillation and solvent analyses were used to calculate component material balances. The Technology and Materials Department has used these results in a separate study comparing experimental K-values and vapor/liquid split with CHAMP computer program design predictions.

Gray, J. A.; Mathias, S. T.

1980-10-01

38

49 CFR 570.56 - Vacuum brake assist unit and vacuum brake system.  

Code of Federal Regulations, 2011 CFR

...pedal. (1) Inspection procedure. Stop the engine and apply service brake several times to destroy vacuum in system. Depress the brake pedal with 50 pounds of force and while maintaining that force, start the engine. If the brake pedal does...

2011-10-01

39

49 CFR 570.56 - Vacuum brake assist unit and vacuum brake system.  

Code of Federal Regulations, 2010 CFR

...Inspection procedure. (i) Check the trailer vacuum system by coupling trailer(s) to truck or truck tractor and opening trailer shutoff valves. Start the engine...indicator activation. (ii) For a combination vehicle equipped with...

2010-10-01

40

Improved synthesis of [(18)F]FLETT via a fully automated vacuum distillation method for [(18)F]2-fluoroethyl azide purification.  

PubMed

The synthesis of [(18)F]2-fluoroethyl azide and its subsequent click reaction with 5-ethynyl-2'-deoxyuridine (EDU) to form [(18)F]FLETT was performed using an iPhase FlexLab module. The implementation of a vacuum distillation method afforded [(18)F]2-fluoroethyl azide in 87±5.3% radiochemical yield. The use of Cu(CH3CN)4PF6 and TBTA as catalyst enabled us to fully automate the [(18)F]FLETT synthesis without the need for the operator to enter the radiation field. [(18)F]FLETT was produced in higher overall yield (41.3±6.5%) and shorter synthesis time (67min) than with our previously reported manual method (32.5±2.5% in 130min). PMID:25113535

Ackermann, Uwe; Plougastel, Lucie; Goh, Yit Wooi; Yeoh, Shinn Dee; Scott, Andrew M

2014-12-01

41

Cascade Distillation Subsystem Development: Progress Toward a Distillation Comparison Test  

NASA Technical Reports Server (NTRS)

Recovery of potable water from wastewater is essential for the success of long-duration manned missions to the Moon and Mars. Honeywell International and a team from NASA Johnson Space Center (JSC) are developing a wastewater processing subsystem that is based on centrifugal vacuum distillation. The wastewater processor, referred to as the Cascade Distillation Subsystem (CDS), utilizes an innovative and efficient multistage thermodynamic process to produce purified water. The rotary centrifugal design of the system also provides gas/liquid phase separation and liquid transport under microgravity conditions. A five-stage subsystem unit has been designed, built, delivered and integrated into the NASA JSC Advanced Water Recovery Systems Development Facility for performance testing. A major test objective of the project is to demonstrate the advancement of the CDS technology from the breadboard level to a subsystem level unit. An initial round of CDS performance testing was completed in fiscal year (FY) 2008. Based on FY08 testing, the system is now in development to support an Exploration Life Support (ELS) Project distillation comparison test expected to begin in early 2009. As part of the project objectives planned for FY09, the system will be reconfigured to support the ELS comparison test. The CDS will then be challenged with a series of human-gene-rated waste streams representative of those anticipated for a lunar outpost. This paper provides a description of the CDS technology, a status of the current project activities, and data on the system s performance to date.

Callahan, M. R.; Lubman, A.; Pickering, Karen D.

2009-01-01

42

Catalytic Distillation  

E-print Network

Catalytic Distillation' refers to a chemical process which performs both a catalyzed reaction and primary fractionation of the reaction components simultaneously. A structured catalyst which also is an effective distillation component has been...

Smith, L. A., Jr.; Hearn, D.; Wynegar, D. P.

1984-01-01

43

27 CFR 26.36c - Shipments of bulk distilled spirits to the United States without payment of tax.  

Code of Federal Regulations, 2012 CFR

...from customs custody to the bonded premises of a distilled spirits plant qualified under part 19 of this chapter. Such shipments are subject to the provisions of subpart Ib. [T.D. ATF-62, 44 FR 71709, Dec. 11,...

2012-04-01

44

27 CFR 26.36c - Shipments of bulk distilled spirits to the United States without payment of tax.  

Code of Federal Regulations, 2010 CFR

...from customs custody to the bonded premises of a distilled spirits plant qualified under part 19 of this chapter. Such shipments are subject to the provisions of subpart Ib. [T.D. ATF-62, 44 FR 71709, Dec. 11,...

2010-04-01

45

27 CFR 26.36c - Shipments of bulk distilled spirits to the United States without payment of tax.  

Code of Federal Regulations, 2011 CFR

...from customs custody to the bonded premises of a distilled spirits plant qualified under part 19 of this chapter. Such shipments are subject to the provisions of subpart Ib. [T.D. ATF-62, 44 FR 71709, Dec. 11,...

2011-04-01

46

27 CFR 26.36c - Shipments of bulk distilled spirits to the United States without payment of tax.  

Code of Federal Regulations, 2013 CFR

...from customs custody to the bonded premises of a distilled spirits plant qualified under part 19 of this chapter. Such shipments are subject to the provisions of subpart Ib. [T.D. ATF-62, 44 FR 71709, Dec. 11,...

2013-04-01

47

27 CFR 26.36c - Shipments of bulk distilled spirits to the United States without payment of tax.  

...from customs custody to the bonded premises of a distilled spirits plant qualified under part 19 of this chapter. Such shipments are subject to the provisions of subpart Ib. [T.D. ATF-62, 44 FR 71709, Dec. 11,...

2014-04-01

48

Advanced Distillation Final Report  

SciTech Connect

The Advanced Distillation project was concluded on December 31, 2009. This U.S. Department of Energy (DOE) funded project was completed successfully and within budget during a timeline approved by DOE project managers, which included a one year extension to the initial ending date. The subject technology, Microchannel Process Technology (MPT) distillation, was expected to provide both capital and operating cost savings compared to conventional distillation technology. With efforts from Velocys and its project partners, MPT distillation was successfully demonstrated at a laboratory scale and its energy savings potential was calculated. While many objectives established at the beginning of the project were met, the project was only partially successful. At the conclusion, it appears that MPT distillation is not a good fit for the targeted separation of ethane and ethylene in large-scale ethylene production facilities, as greater advantages were seen for smaller scale distillations. Early in the project, work involved flowsheet analyses to discern the economic viability of ethane-ethylene MPT distillation and develop strategies for maximizing its impact on the economics of the process. This study confirmed that through modification to standard operating processes, MPT can enable net energy savings in excess of 20%. This advantage was used by ABB Lumus to determine the potential impact of MPT distillation on the ethane-ethylene market. The study indicated that a substantial market exists if the energy saving could be realized and if installed capital cost of MPT distillation was on par or less than conventional technology. Unfortunately, it was determined that the large number of MPT distillation units needed to perform ethane-ethylene separation for world-scale ethylene facilities, makes the targeted separation a poor fit for the technology in this application at the current state of manufacturing costs. Over the course of the project, distillation experiments were performed with the targeted mixture, ethane-ethylene, as well as with analogous low relative volatility systems: cyclohexane-hexane and cyclopentane-pentane. Devices and test stands were specifically designed for these efforts. Development progressed from experiments and models considering sections of a full scale device to the design, fabrication, and operation of a single-channel distillation unit with integrated heat transfer. Throughout the project, analytical and numerical models and Computational Fluid Dynamics (CFD) simulations were validated with experiments in the process of developing this platform technology. Experimental trials demonstrated steady and controllable distillation for a variety of process conditions. Values of Height-to-an-Equivalent Theoretical Plate (HETP) ranging from less than 0.5 inch to a few inches were experimentally proven, demonstrating a ten-fold performance enhancement relative to conventional distillation. This improvement, while substantial, is not sufficient for MPT distillation to displace very large scale distillation trains. Fortunately, parallel efforts in the area of business development have yielded other applications for MPT distillation, including smaller scale separations that benefit from the flowsheet flexibility offered by the technology. Talks with multiple potential partners are underway. Their outcome will also help determine the path ahead for MPT distillation.

Maddalena Fanelli; Ravi Arora; Annalee Tonkovich; Jennifer Marco; Ed Rode

2010-03-24

49

Distill, Distill_roll Distill for CASP10  

E-print Network

Distill, Distill_roll Distill for CASP10 C. Mirabello1, G. Tradigo1,2 , P.Veltri2, and G. Pollastri and Distill_roll is that for the former we use an improved fold recognition algorithm. Methods Distill runs 3 through 3 searches for Distill_roll (PSSM and SAMD profile against PDB sequences and SAMD, with 3

Pollastri, Gianluca

50

Radioactive air emissions notice of construction HEPA filtered vacuum radioactive air emission units  

SciTech Connect

This notice of construction (NOC) requests a categorical approval for construction and operation of certain portable high-efficiency particulate air (HEPA) filtered vacuum radionuclide airborne emission units (HVUs). Approval of this NOC application is intended to allow operation of the HVUs without prior project-specific approval. This NOC does not request replacement or supersedence of any previous agreements/approvals by the Washington State Department of Health for the use of vacuums on the Hanford Site. These previous agreement/approvals include the approved NOCs for the use of EuroClean HEPA vacuums at the T Plant Complex (routine technical meeting 12/10/96) and the Kelly Decontamination System at the Plutonium-Uranium Extraction (PUREX) Plant (routine technical meeting 06/25/96). Also, this NOC does not replace or supersede the agreement reached regarding the use of HEPA hand-held/shop-vacuum cleaners for routine cleanup activities conducted by the Environmental Restoration Project. Routine cleanup activities are conducted during the surveillance and maintenance of inactive waste sites (Radioactive Area Remedial Action Project) and inactive facilities. HEPA hand-held/shop-vacuum cleaners are used to clean up spot surface contamination areas found during outdoor radiological field surveys, and to clean up localized radiologically contaminated material (e.g., dust, dirt, bird droppings, animal feces, liquids, insects, spider webs, etc.). This agreement, documented in the October 12, 1994 Routine Meeting Minutes, is based on routine cleanup consisting of spot cleanup of low-level contamination provided that, in each case, the source term potential would be below 0.1 millirem per year.

JOHNSON, R.E.

1999-09-01

51

Solar Distillation  

Microsoft Academic Search

\\u000a “Solar distillation” is a technology for producing potable water from brackish and underground water of low-quality at low\\u000a cost. It can reduce water-scarcity problems together with other water purification technologies. Solar distillation is analogous\\u000a to natural hydrological cycle. It uses an apparatus called a solar still in which water is evaporated using solar energy,\\u000a a form of renewable energy, and

Rahul Dev; Gopal Nath Tiwari

52

Design and Optimization of Condenser and Centrifuge Units for Enhancement of a Batch Vacuum Frying System  

E-print Network

of the product under vacuum, which make the product healthier than what is currently available. The de-oiling mechanism consists of a centrifuge with a motor attached to the basket shaft, rotating up to 750 rpm (63 g units). The condenser consists of a... (counter- flow) spiral-coil heat exchanger (SHE) connected to a refrigeration system that uses R404a refrigerant. De-oiling for 40 s at 300 and 750 RPM removed up to 67% and 72% of the chip?s surface oil, respectively. At 750 RPM for 10 s, 40 s, and 60...

Pandey, Akhilesh

2011-02-22

53

Distillation of Bell states in open systems  

SciTech Connect

In this work we show that the distillation protocol proposed by P. Chen et al. [Phys. Rev. A 54, 3824 (1996)] allows one to distill Bell states at any time for a system evolving in vacuum and prepared in an initial singlet. It is also shown that the same protocol, applied in nonzero temperature thermal baths, yields a considerable recovering of entanglement.

Isasi, E.; Mundarain, D. [Departamento de Fisica, Seccion de Fenomenos Opticos, Universidad Simon Bolivar, Apartado Postal 89000, Caracas 1080A (Venezuela, Bolivarian Republic of)

2010-04-15

54

Process for the preparation of light hydrocarbon distillates by hydrocracking and catalytic cracking  

SciTech Connect

This patent describes a process for the preparation of a gasoline range petroleum distillate from a vacuum heavy hydrocarbon oil distillate. It comprises: passing at least a portion of the vacuum heavy hydrocarbon oil distillate to a hydrocracking zone to hydrocrack the distillate into a product stream comprising a hydrocracked distillate residue having an initial boiling point of at least 300{sup 0}C; passing the hydrocracked distillate to a distillation separation zone to separate and recover the residue; passing the residue to a catalytic cracking zone to catalytically crack the residue; passing at least a portion of the vacuum heavy oil distillate prior to hydrocracking to the catalytic cracking to catalytically crack the vacuum heaving oil distillate; withdrawing the gasoline range petroleum distillate from the catalytic cracking zone.

DeVries, A.F.; Stork, W.H.J.

1989-08-22

55

Filament-strung stand-off elements for maintaining pane separation in vacuum insulating glazing units  

DOEpatents

A vacuum insulating glazing unit (VIGU) comprises first and second panes of transparent material, first and second anchors, a plurality of filaments, a plurality of stand-off elements, and seals. The first and second panes of transparent material have edges and inner and outer faces, are disposed with their inner faces substantially opposing one another, and are separated by a gap having a predetermined height. The first and second anchors are disposed at opposite edges of one pane of the VIGU. Each filament is attached at one end to the first anchor and at the other end to the second anchor, and the filaments are collectively disposed between the panes substantially parallel to one another. The stand-off elements are affixed to each filament at predetermined positions along the filament, and have a height substantially equal to the predetermined height of the gap such that the each stand-off element touches the inner surfaces of both panes. The seals are disposed about the edges of the panes, enclosing the stand-off elements within a volume between the panes from which the atmosphere may be evacuated to form a partial vacuum.

Bettger, Kenneth J; Stark, David H

2013-08-20

56

Analyzing the contents of residual and plasma-supporting gases inside a vacuum deposition unit chamber  

NASA Astrophysics Data System (ADS)

The paper describes a quadruple mass-spectrometer method, which is used to analyze the content of residual gas in a vacuum chamber of the ARM NTM (Automatised Working Area) ion-plasma unit. This unit is used to perfect the magnetron deposition process for coating radio-reflecting surfaces. The intake of pure argon into the chamber revealed up to 0.3 % of impurities in the plasma-supporting gas, including 0.02 % of water and oxygen. A significant presence of hydrocarbon gases is explained by the presence of solvents sorbed in rubber washers, joints of internal equipment, and other components inside the chamber. In order to decrease the level of impurities in the plasmasupporting atmosphere inside the chamber and improve the composition and properties of the coatings, it is necessary to take additional measures to cleanse and degas the surface of the chamber from condensation products and hydrocarbon compounds. To provide a minimal level of impurities in the coated surfaces it is vital to clean and degas the surfaces of the chamber, removing residual moisture and hydrocarbon compounds.

Mikheev, A. Ye; Kharlamov, V. A.; Kruchek, S. D.; Cherniatina, A. A.; Khomenko, I. I.

2015-01-01

57

Vacuum Induction Melting Unit Induction heating is a process wherein induced eddy currents heat conductive materials. This heating  

E-print Network

Vacuum Induction Melting Unit Induction heating is a process wherein induced eddy currents heat field and circulating eddy currents are induced within the metals. Flow of eddy currents leads an AC current through a water cooled copper coil and a metallic charge is placed in a ceramic (or

Subramaniam, Anandh

58

Revamp for more middle distillate  

SciTech Connect

In view of the continued decline in demand for residual fuel oil, the much publicised tightness of refining margins and hence funds for new investment, it is appropriate at this time to review some relatively inexpensive, but well-proven, revamp options that are available to the refiner for increasing yields of mid-distillate products at the expense of fuel oil components. With the partial or complete closure of so much refining capacity, much surplus equipment is available for implementing revamp projects. There is also scope for revamping hitherto moth-balled units and operating them in a manner different from that envisaged during their original design. Some long established conversion processes such as visbreaking and thermal cracking can enjoy a renaissance if demand for distillates remains strong. Mild hydrocracking and distillate dewaxing which are more recent developments in refinery processing can also figure prominently in plans for incremental production of middle distillates.

Weeks, D.J.; Pierce, V.E.

1985-03-01

59

Catalytic distillation structure  

DOEpatents

Catalytic distillation structure for use in reaction distillation columns, a providing reaction sites and distillation structure and consisting of a catalyst component and a resilient component intimately associated therewith. The resilient component has at least about 70 volume % open space and being present with the catalyst component in an amount such that the catalytic distillation structure consist of at least 10 volume % open space.

Smith, Jr., Lawrence A. (Bellaire, TX)

1984-01-01

60

Performance Characterization and Simulation of Amine-Based Vacuum Swing Sorption Units for Spacesuit Carbon Dioxide and Humidity Control  

NASA Technical Reports Server (NTRS)

Controlling carbon dioxide (CO2) and water (H2O) vapor concentrations in a space suit is critical to ensuring an astronauts safety, comfort, and capability to perform extra-vehicular activity (EVA) tasks. Historically, this has been accomplished using lithium hydroxide (LiOH) and metal oxide (MetOx) canisters. Lithium hydroxide is a consumable material that requires priming with water before it becomes effective at removing carbon dioxide. MetOx is regenerable through a power-intensive thermal cycle but is significantly heavier on a volume basis than LiOH. As an alternative, amine-based vacuum swing beds are under aggressive development for EVA applications. The vacuum swing units control atmospheric concentrations of both CO2 and H2O through fully-regenerative process. The current concept, referred to as the rapid cycle amine (RCA), has resulted in numerous laboratory prototypes. Performance of these prototypes have been assessed experimentally and documented in previous reports. To support developmental e orts, a first principles model has also been established for the vacuum swing sorption technology. For the first time in several decades, a major re-design of Portable Life Support System (PLSS) for the extra-vehicular mobility unit (EMU) is underway. NASA at Johnson Space Center built and tested an integrated PLSS test bed of all subsystems under a variety of simulated EVA conditions of which the RCA prototype played a significant role. The efforts documented herein summarize RCA test performance and simulation results for single and variable metabolic rate experiments in an integrated context. In addition, a variety of off-nominal tests were performed to assess the capability of the RCA to function under challenging circumstances. Tests included high water production experiments, degraded vacuum regeneration, and deliberate valve/power failure and recovery.

Swickrath, Michael J.; Watts, Carly; Anderson, Molly; McMillin, Summer; Broerman, Craig; Colunga, Aaron; Vogel, Matthew

2012-01-01

61

Extended testing of compression distillation.  

NASA Technical Reports Server (NTRS)

During the past eight years, the NASA Manned Spacecraft Center has supported the development of an integrated water and waste management system which includes the compression distillation process for recovering useable water from urine, urinal flush water, humidity condensate, commode flush water, and concentrated wash water. This paper describes the design of the compression distillation unit, developed for this system, and the testing performed to demonstrate its reliability and performance. In addition, this paper summarizes the work performed on pretreatment and post-treatment processes, to assure the recovery of sterile potable water from urine and treated urinal flush water.

Bambenek, R. A.; Nuccio, P. P.

1972-01-01

62

Solar distillation of sea water  

SciTech Connect

Indian coastal and fishing villages suffer from scarcity of potable water. Solar distillation could provide a solution to this problem by adopting the following criteria: (1) Integration of distillation and storage systems with the house design. (2) Public supply of sea water and a public drain pipe system to periodically drain away the concentrated brine. (3) Harvest and store rain water to tide over cloudy rainy periods. In India there has been a thrust towards centralized non-conventional energy systems. Decentralized non-conventional energy devices and centralized service support units may offer a better solution. 1 fig.

Subramanyam, S. (Kakatiya Institute of Technology and Science, Warangal (India))

1989-01-01

63

Catalytic distillation structure  

DOEpatents

Catalytic distillation structure is described for use in reaction distillation columns, and provides reaction sites and distillation structure consisting of a catalyst component and a resilient component intimately associated therewith. The resilient component has at least about 70 volume % open space and is present with the catalyst component in an amount such that the catalytic distillation structure consists of at least 10 volume % open space. 10 figs.

Smith, L.A. Jr.

1984-04-17

64

Vacuum Technology  

SciTech Connect

The environmental condition called vacuum is created any time the pressure of a gas is reduced compared to atmospheric pressure. On earth we typically create a vacuum by connecting a pump capable of moving gas to a relatively leak free vessel. Through operation of the gas pump the number of gas molecules per unit volume is decreased within the vessel. As soon as one creates a vacuum natural forces (in this case entropy) work to restore equilibrium pressure; the practical effect of this is that gas molecules attempt to enter the evacuated space by any means possible. It is useful to think of vacuum in terms of a gas at a pressure below atmospheric pressure. In even the best vacuum vessels ever created there are approximately 3,500,000 molecules of gas per cubic meter of volume remaining inside the vessel. The lowest pressure environment known is in interstellar space where there are approximately four molecules of gas per cubic meter. Researchers are currently developing vacuum technology components (pumps, gauges, valves, etc.) using micro electro mechanical systems (MEMS) technology. Miniature vacuum components and systems will open the possibility for significant savings in energy cost and will open the doors to advances in electronics, manufacturing and semiconductor fabrication. In conclusion, an understanding of the basic principles of vacuum technology as presented in this summary is essential for the successful execution of all projects that involve vacuum technology. Using the principles described above, a practitioner of vacuum technology can design a vacuum system that will achieve the project requirements.

Biltoft, P J

2004-10-15

65

Design and evaluation of dynamic equivalent test platform for thermal vacuum qualification test of docking units  

NASA Astrophysics Data System (ADS)

In this paper, a dynamic equivalent test platform for large-mass spacecraft docking in thermal vacuum has been successfully developed. An equivalent-mass docking test principle for reducing the size of the test platform has been introduced. In addition, by adopting a flywheel to simulate part equivalent mass of docking test, the scheme of making a more compact test platform has been realized. Furthermore, the identification of the friction force in the platform to guarantee the equivalent velocity of docking test has been demonstrated. At last, the performance of the test platform has been evaluated through both the docking simulation with software and the docking test on the platform. The results of comparison between the docking simulations and the experimental tests proved the effectiveness of the equivalent-mass docking test principle and also indicated that the docking test platform developed in this work has the ability to simulate the docking process precisely.

Zhu, Yanhe; Fan, Jizhuang; Wang, Xiaolu; Zhang, Yu; Zhao, Jie

2015-01-01

66

Vacuum pump aids ejectors  

SciTech Connect

The steam ejector/vacuum pump hybrid system has been operating satisfactorily since the summer of 1981. This system has essentially been as troublefree as the all-ejector system and, of course, has provided a substantial cost savings. Construction is currently under way to convert the vacuum system of another crude still which is equipped with steam ejectors and barometric condensers to the hybrid system of steam ejectors, surface condensers, and vacuum pumps. This current project is even more financially attractive because it allows a dirty water cooling tower which serves the barometric condensers to be shut down. Providing a vacuum for crude distillation vacuum towers with this hybrid system is by no means the only application of this technique. Any vacuum system consisting of all steam ejectors would be a candidate for this hybrid system and the resulting savings in energy.

Nelson, R.E.

1982-12-01

67

COR1 Engineering Test Unit Measurements at the NCAR/HAO Vacuum Tunnel Facility, October-November 2002  

NASA Technical Reports Server (NTRS)

The Engineering Test Unit (ETU) of COR1 was made in two configurations. The first configuration, ETU-1, was for vibration testing, while the second, ETU-2, was for optical testing. This is a report on the optical testing performed on ETU-2 at the NCAR/HAO Vacuum Tunnel Facility during the months of October and November, 2002. This was the same facility used to test the two previous breadboard models. In both configurations, the first two tube sections were complete, with all optical elements aligned. The vibration model ETU-1 had the remaining tube sections attached, with mass models for the remaining optics, for the various mechanisms, and for the focal plane assembly. It was then converted into the optical model ETU-2 by removing tube sections 3 to 5, and mounting the remaining optics on commercial mounts. (The bandpass filter was also installed into tube 2, which had been replaced in ETU-1 by a mass model, so that pre- and post-vibration optical measurements could be made.) Doublet 2 was installed in a Newport LP-2 carrier, and aligned to the other optics in the first two tube sections. The LP-2 adjustment screws were then uralened so that the alignment could be maintained during shipping. Because neither the flight polarizer nor Hollow Core Motor were available, they were simulated by a commercial polarizer and rotational mount, both from Oriel corporation. The Oriel rotational stage was not designed for vacuum use, but it was determined after consultation with the company, and lab testing, that the stage could be used in the moderate vacuum conditions at the NCAR/HAO facility. The shutter and focal plane assembly were simulated with the same camera used for the previous two breadboard tests. The focal plane mask was simulated with a plane of BK7 glass with a mask glued on, using the same procedure as for the Lyot spot on Doublet 1, and mounted in an adjustable LP-2 carrier. Two masks were made, one made to the precise specifications of the optical design, the other slightly bigger to make alignment easier.

Thompson, William

2002-01-01

68

Catalytic distillation process  

DOEpatents

A method is described for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contacting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C[sub 4] feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.

Smith, L.A. Jr.

1982-06-22

69

Catalytic distillation process  

DOEpatents

A method for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contacting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C.sub.4 feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.

Smith, Jr., Lawrence A. (Bellaire, TX)

1982-01-01

70

27 CFR 27.1 - Imported distilled spirits, wines, and beer.  

Code of Federal Regulations, 2012 CFR

...distilled spirits, wines, and beer into the United States from foreign countries including commodity taxes, permits, marking, branding, closing and labeling of containers and packages, and records and reports. Note: Distilled spirits, wines,...

2012-04-01

71

27 CFR 27.1 - Imported distilled spirits, wines, and beer.  

Code of Federal Regulations, 2013 CFR

...distilled spirits, wines, and beer into the United States from foreign countries including commodity taxes, permits, marking, branding, closing and labeling of containers and packages, and records and reports. Note: Distilled spirits, wines,...

2013-04-01

72

27 CFR 27.1 - Imported distilled spirits, wines, and beer.  

...distilled spirits, wines, and beer into the United States from foreign countries including commodity taxes, permits, marking, branding, closing and labeling of containers and packages, and records and reports. Note: Distilled spirits, wines,...

2014-04-01

73

Energy Saving in Distillation Using Structured Packing and Vapor Recompression  

E-print Network

distillation application, a column with a small pressure drop is especially important. An example of a vacuum distillation which is made suitable for VRC with use of structured packing is sep~ration of styrene and ethylbenzene. Approximately 70...% of the world's styrene capac ty is now processed through columns filled with Flex pac? or Mellapak structured packings. In conventio al column operation, energy savings of 20 to 30% re obtained by replacing trays or dumped packings Other benefits...

Hill, J.H.

74

Preprototype Vapor Compression Distillation Subsystem development  

NASA Technical Reports Server (NTRS)

Vapor Compression Distillation (VCD) has evolved as the most promising approach to reclaim potable water from wastewater for future long-term manned space missions. Life Systems, Inc. (LSI), working with NASA, has developed a preprototype Vapor Compression Distillation Subsystem (VCDS) which processes wastewater at 1.4 kg/h. The preprototype unit weighs 143 kg, occupies a volume of 0.47 cu m, and will reclaim 96 percent of the available wastewater. This unit has been tested by LSI and is scheduled for further testing at NASA-JSC. This paper presents the preprototype VCDS design, configuration, performance data, test results and flight system projections.

Thompson, C. D.; Ellis, G. S.; Schubert, F. H.

1981-01-01

75

Datalogging the Distillation Process.  

ERIC Educational Resources Information Center

Presents a distillation experiment that uses temperature sensors connected to a computer in place of thermometers, and enables the whole class to view the data on a monitor and interpret and discuss the data in real time. (JRH)

Soares, Allan; Creevy, Steven

1995-01-01

76

40 CFR 721.4500 - Isopropylamine distillation residues and ethylamine distillation residues.  

Code of Federal Regulations, 2010 CFR

... 2010-07-01 false Isopropylamine distillation residues and ethylamine distillation residues. 721.4500 Section 721...Substances § 721.4500 Isopropylamine distillation residues and ethylamine distillation...

2010-07-01

77

40 CFR 721.4500 - Isopropylamine distillation residues and ethylamine distillation residues.  

Code of Federal Regulations, 2011 CFR

... 2011-07-01 false Isopropylamine distillation residues and ethylamine distillation residues. 721.4500 Section 721...Substances § 721.4500 Isopropylamine distillation residues and ethylamine distillation...

2011-07-01

78

Distillation device supplies cesium vapor at constant pressure  

NASA Technical Reports Server (NTRS)

Distillation apparatus in the form of a U tube supplies small amounts of pure cesium vapor at constant pressure to a thermionic converter. The upstream leg of the U tube is connected to a vacuum pump to withdraw noncondensable impurities, the bottom portion serves as a reservoir for the liquid cesium.

Basiulis, A.; Shefsiek, P. K.

1968-01-01

79

Topological quantum distillation.  

PubMed

We construct a class of topological quantum codes to perform quantum entanglement distillation. These codes implement the whole Clifford group of unitary operations in a fully topological manner and without selective addressing of qubits. This allows us to extend their application also to quantum teleportation, dense coding, and computation with magic states. PMID:17155532

Bombin, H; Martin-Delgado, M A

2006-11-01

80

27 CFR 27.40 - Distilled spirits.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 2010-04-01 false Distilled spirits. 27.40 Section 27.40 Alcohol...TREASURY LIQUORS IMPORTATION OF DISTILLED SPIRITS, WINES, AND BEER Tax On Imported Distilled Spirits, Wines, and Beer Distilled Spirits...

2010-04-01

81

AMMONIA DISTILLATION FOR DEUTERIUM SEPARATION  

Microsoft Academic Search

The relative volatility or separation factor for deuterium enrichment in ; ammonia distillation was measured at several pressures and deuterium ; concentrations. The knowledge of this ingormation is very helpful in predicting ; costs of heawy water production by the ammonia distillation process. It hss been ; stated by others, that the ammonia distillation process of heawy water production ;

G. T. Petersen; M. Benedict

1960-01-01

82

Recycling of acetone by distillation  

SciTech Connect

The Resource Conservation Recovery Act (RCRA) identifies spent acetone solvent as a listed hazardous waste. At Fernald, acetone has been spent that has been contaminated with radionuclides and therefore is identified as a mixed hazardous waste. At the time of this publication there is no available approved method of recycling or disposal of radioactively contaminated spent acetone solvent. The Consent Decree with the Ohio EPA and the Consent Agreement with the United States EPA was agreed upon for the long-term compliant storage of hazardous waste materials. The purpose of this project was to demonstrate the feasibility for safely decontaminating spent acetone to background levels of radioactivity for reuse. It was postulated that through heat distillation, radionuclides could be isolated from the spent acetone.

Brennan, D.L.; Campbell, B.A.; Phelan, J.E.; Harper, M.

1992-09-01

83

Cascade Distillation System Development  

NASA Technical Reports Server (NTRS)

NASA's Advanced Exploration Systems (AES) Life Support System (LSS) Project is chartered with de-veloping advanced life support systems that will ena-ble NASA human exploration beyond low Earth orbit (LEO). The goal of AES is to increase the affordabil-ity of long-duration life support missions, and to re-duce the risk associated with integrating and infusing new enabling technologies required to ensure mission success. Because of the robust nature of distillation systems, the AES LSS Project is pursuing develop-ment of the Cascade Distillation Subsystem (CDS) as part of its technology portfolio. Currently, the system is being developed into a flight forward Generation 2.0 design.

Callahan, Michael R.; Sargushingh, Miriam; Shull, Sarah

2014-01-01

84

Microchannel Distillation of JP-8 Jet Fuel for Sulfur Content Reduction  

SciTech Connect

In microchannel based distillation processes, thin vapor and liquid films are contacted in small channels where mass transfer is diffusion-limited. The microchannel architecture enables improvements in distillation processes. A shorter height equivalent of a theoretical plate (HETP) and therefore a more compact distillation unit can be achieved. A microchannel distillation unit was used to produce a light fraction of JP-8 fuel with reduced sulfur content for use as feed to produce fuel-cell grade hydrogen. The HETP of the microchannel unit is discussed, as well as the effects of process conditions such as feed temperature, flow rate, and reflux ratio.

Zheng, Feng; Stenkamp, Victoria S.; TeGrotenhuis, Ward E.; Huang, Xiwen; King, David L.

2006-09-16

85

Desalination Using Vapor-Compression Distillation  

E-print Network

to thank my committee members, Dr. Barrufet and Dr. El- Halwagi, for their guidance throughout the completion of this research. I am truly grateful to Dr. Jorge Lara, the faculty, and the staff of the Chemical Engineering Department of Texas A... is commonly used for small- and medium-scale desalination units. There are two methods to compress the vapor: mechanical compressors and steam jets. Lara [6] states that mechanical vapor compression is very efficient. Unlike other distillation systems...

Lubis, Mirna R.

2010-07-14

86

Improved waste water vapor compression distillation technology. [for Spacelab  

NASA Technical Reports Server (NTRS)

The vapor compression distillation process is a method of recovering potable water from crewman urine in a manned spacecraft or space station. A description is presented of the research and development approach to the solution of the various problems encountered with previous vapor compression distillation units. The design solutions considered are incorporated in the preliminary design of a vapor compression distillation subsystem. The new design concepts are available for integration in the next generation of support systems and, particularly, the regenerative life support evaluation intended for project Spacelab.

Johnson, K. L.; Nuccio, P. P.; Reveley, W. F.

1977-01-01

87

Vacuum Camera Cooler  

NASA Technical Reports Server (NTRS)

Acquiring cheap, moving video was impossible in a vacuum environment, due to camera overheating. This overheating is brought on by the lack of cooling media in vacuum. A water-jacketed camera cooler enclosure machined and assembled from copper plate and tube has been developed. The camera cooler (see figure) is cup-shaped and cooled by circulating water or nitrogen gas through copper tubing. The camera, a store-bought "spy type," is not designed to work in a vacuum. With some modifications the unit can be thermally connected when mounted in the cup portion of the camera cooler. The thermal conductivity is provided by copper tape between parts of the camera and the cooled enclosure. During initial testing of the demonstration unit, the camera cooler kept the CPU (central processing unit) of this video camera at operating temperature. This development allowed video recording of an in-progress test, within a vacuum environment.

Laugen, Geoffrey A.

2011-01-01

88

Distillation: The Efficient Workhorse  

E-print Network

aT Possible First glance may show only 3 or 4 utility levels (temperatures) to choose from. These might well be 1000e apart. Some ways to increase the options are: ' multieffect distillation (this spreads the 6T across 2 or 3 towers) use of waste heat...). Cooling below top? Liquid composition Heating above bottom FIG. 3 INTERNED lATE CONDENSER AND REBOILER Plax efficiency Max ett'iclenc)' SO, of heavy 95' of heavy component in component In feed teed 1 condenser r 1 [eboiler 67 20 2 con6ensers r 1...

Steinmeyer, D.

89

75 FR 81949 - Disclosure of Cochineal Extract and Carmine in the Labeling of Wines, Distilled Spirits, and Malt...  

Federal Register 2010, 2011, 2012, 2013

...Carmine in the Labeling of Wines, Distilled Spirits, and Malt Beverages; Comment Period...Carmine in the Labeling of Wines, Distilled Spirits, and Malt Beverages, a notice of proposed...Lynne J. Omlie on behalf of the Distilled Spirits Council of the United States,...

2010-12-29

90

Performance Characterization and Simulation of Amine-Based Vacuum Swing Adsorption Units for Spacesuit Carbon Dioxide and Humidity Control  

NASA Technical Reports Server (NTRS)

Controlling carbon dioxide (CO2) and water (H2O) concentrations in the vapor phase of a space suit is critical to ensuring an astronauts safety, comfortability, and capability to perform extra-vehicular activity (EVA) tasks. Historically, this has been accomplished using lithium hydroxide (LiOH) and metal oxides (MetOx). Lithium hydroxide is a consumable material and requires priming with water before it becomes effective at removing carbon dioxide. MetOx is regenerable through a power-intensive thermal cycle but is significantly heavier on a volume basis than LiOH. As an alternative, amine-based vacuum swing beds are under aggressive development for EVA applications which control atmospheric concentrations of both CO2 and H2O through a fully-regenerative process. The current concept, referred to as the rapid cycle amine (RCA), has resulted in numerous laboratory prototypes. Performance of these prototypes have been assessed and documented from experimental and theoretical perspectives. To support developmental efforts, a first principles model has also been established for the vacuum swing adsorption technology. The efforts documented herein summarize performance characterization and simulation results for several variable metabolic profiles subjected to the RCA. Furthermore, a variety of control methods are explored including timed swing cycles, instantaneous CO2 feedback control, and time-averaged CO2 feedback control. A variety of off-nominal tests are also explored including high/low suit temperatures, increasingly high humidity cases, and dynamic pressure cases simulating the suit pre-breathe protocol. Consequently, this work builds on efforts previous efforts to fully bound the performance of the rapid cycle amine under a variety of nominal and off-nominal conditions.

Swickrath, Michael J.; Watts,Carly; Anderson, Molly; McMillin, Summer; Boerman, Craig; Colunga, Aaron; Vogel, Matthew

2011-01-01

91

Propellant Analysis and Distillation Unit Design  

NASA Technical Reports Server (NTRS)

The NASA White Sands Test Facility (WSTF) routinely operates hypergolic propulsion systems. Some of the onsite activities include performing long duration studies on the operational life of these systems. A few of them have been in use for over twenty years. During this span of time contamination has built up in the propellant and some of the distribution infrastructure. This study investigated the nature of this contamination, the pathology of its generation, and developed a process for removal of the contamination that was cost efficient with minimal waste generation.

Barragan, Michelle H.; Spangler, Cindy; Barrera, Louis K.

2007-01-01

92

Crude Distillation Unit Heat Recovery Study  

E-print Network

study. However, ways were found to overcome the limitations and make it work. It did produce what appears to be a good result; with reasonable shell counts and logical flow patterns. Project Facilities PREFRACT ATMOS VAC 1 VAC 2 , . ~ ?~ 150P STM...

John, P.

1979-01-01

93

27 CFR 19.301 - Distillation.  

Code of Federal Regulations, 2013 CFR

...ALCOHOL DISTILLED SPIRITS PLANTS Production of Distilled Spirits Rules...through the various steps of production as quickly as plant operation will permit...many distilling or other production operations as...

2013-04-01

94

27 CFR 19.301 - Distillation.  

Code of Federal Regulations, 2011 CFR

...LIQUORS DISTILLED SPIRITS PLANTS Production of Distilled Spirits Rules...through the various steps of production as quickly as plant operation will permit...many distilling or other production operations as...

2011-04-01

95

27 CFR 19.301 - Distillation.  

Code of Federal Regulations, 2012 CFR

...LIQUORS DISTILLED SPIRITS PLANTS Production of Distilled Spirits Rules...through the various steps of production as quickly as plant operation will permit...many distilling or other production operations as...

2012-04-01

96

27 CFR 19.301 - Distillation.  

...ALCOHOL DISTILLED SPIRITS PLANTS Production of Distilled Spirits Rules...through the various steps of production as quickly as plant operation will permit...many distilling or other production operations as...

2014-04-01

97

27 CFR 19.316 - Distillation.  

Code of Federal Regulations, 2010 CFR

...LIQUORS DISTILLED SPIRITS PLANTS Production § 19.316 Distillation...many distilling or other production operations as desired...through the various steps of production as expeditiously as plant operation will...

2010-04-01

98

27 CFR 24.216 - Distilling material.  

Code of Federal Regulations, 2012 CFR

...material, using any quantity of water desired to facilitate fermentation or distillation. No sugar may be added in the production...material. Distillates containing aldehydes may be used in the fermentation of wine to be used as distilling material. Lees,...

2012-04-01

99

27 CFR 24.216 - Distilling material.  

Code of Federal Regulations, 2013 CFR

...material, using any quantity of water desired to facilitate fermentation or distillation. No sugar may be added in the production...material. Distillates containing aldehydes may be used in the fermentation of wine to be used as distilling material. Lees,...

2013-04-01

100

27 CFR 24.216 - Distilling material.  

Code of Federal Regulations, 2011 CFR

...material, using any quantity of water desired to facilitate fermentation or distillation. No sugar may be added in the production...material. Distillates containing aldehydes may be used in the fermentation of wine to be used as distilling material. Lees,...

2011-04-01

101

27 CFR 24.216 - Distilling material.  

...material, using any quantity of water desired to facilitate fermentation or distillation. No sugar may be added in the production...material. Distillates containing aldehydes may be used in the fermentation of wine to be used as distilling material. Lees,...

2014-04-01

102

27 CFR 24.216 - Distilling material.  

Code of Federal Regulations, 2010 CFR

...material, using any quantity of water desired to facilitate fermentation or distillation. No sugar may be added in the production...material. Distillates containing aldehydes may be used in the fermentation of wine to be used as distilling material. Lees,...

2010-04-01

103

Vapor compression distillation module  

NASA Technical Reports Server (NTRS)

A Vapor Compression Distillation (VCD) module was developed and evaluated as part of a Space Station Prototype (SSP) environmental control and life support system. The VCD module includes the waste tankage, pumps, post-treatment cells, automatic controls and fault detection instrumentation. Development problems were encountered with two components: the liquid pumps, and the waste tank and quantity gauge. Peristaltic pumps were selected instead of gear pumps, and a sub-program of materials and design optimization was undertaken leading to a projected life greater than 10,000 hours of continuous operation. A bladder tank was designed and built to contain the waste liquids and deliver it to the processor. A detrimental pressure pattern imposed upon the bladder by a force-operated quantity gauge was corrected by rearranging the force application, and design goals were achieved. System testing has demonstrated that all performance goals have been fulfilled.

Nuccio, P. P.

1975-01-01

104

Delayed birth of distillable entanglement in the evolution of bound entangled states  

SciTech Connect

The dynamical creation of entanglement between three-level atoms coupled to the common vacuum is investigated. For the class of bound entangled initial states, we show that the dynamics of closely separated atoms generates stationary distillable entanglement of asymptotic states. We also find that the effect of delayed sudden birth of distillable entanglement occurs in the case of atoms separated by a distance comparable with the radiation wavelength.

Derkacz, Lukasz; Jakobczyk, Lech [Opera Software International AS, Oddzialw Polsce, ul. Szewska 8, 50-122 Wroclaw (Poland); Institute of Theoretical Physics, University of Wroclaw, Plac Maxa Borna 9, 50-204 Wroclaw (Poland)

2010-08-15

105

Delayed birth of distillable entanglement in the evolution of bound entangled states  

E-print Network

The dynamical creation of entanglement between three-level atoms coupled to the common vacuum is investigated. For the class of bound entangled initial states we show that the dynamics of closely separated atoms generates stationary distillable entanglement of asymptotic states. We also find that the effect of delayed sudden birth of distillable entanglement occurs in the case of atoms separated by a distance comparable with the radiation wavelength.

?ukasz Derkacz; Lech Jakobczyk

2010-08-17

106

Extraction of protein from distiller’s grain  

Microsoft Academic Search

We have investigated the feasibility of extracting the oil and protein from distiller’s grain (DG) to obtain a higher-valued protein-rich product and a carbohydrate-rich residue better suited for conversion to fermentable sugars. Protein extractions based on aqueous ethanol, alkaline-ethanol, and aqueous enzyme treatments were compared. Three of the methods extracted a significant amount of the protein from dried, defatted DG

Drew J. Cookman; Charles E. Glatz

2009-01-01

107

Distillation. Third World Science.  

ERIC Educational Resources Information Center

This unit, developed by the Third World Science Project, is designed to add a multicultural element to existing science syllabi (for students aged 11-16) in the United Kingdom. The project seeks to develop an appreciation of the: boundless fascination of the natural world; knowledge, skills, and expertise possessed by men/women everywhere;…

Jones, Natalie; Hughes, Wyn

108

27 CFR 19.307 - Distillates containing extraneous substances.  

... DISTILLED SPIRITS PLANTS Production of Distilled Spirits...substances. (a) Use in production. Distillates...distilling system before the production gauge and promptly...the distilled spirits plant from which the...

2014-04-01

109

27 CFR 19.307 - Distillates containing extraneous substances.  

Code of Federal Regulations, 2011 CFR

... DISTILLED SPIRITS PLANTS Production of Distilled Spirits...substances. (a) Use in production. Distillates...distilling system before the production gauge and promptly...the distilled spirits plant from which the...

2011-04-01

110

27 CFR 19.307 - Distillates containing extraneous substances.  

Code of Federal Regulations, 2013 CFR

... DISTILLED SPIRITS PLANTS Production of Distilled Spirits...substances. (a) Use in production. Distillates...distilling system before the production gauge and promptly...the distilled spirits plant from which the...

2013-04-01

111

27 CFR 19.307 - Distillates containing extraneous substances.  

Code of Federal Regulations, 2012 CFR

... DISTILLED SPIRITS PLANTS Production of Distilled Spirits...substances. (a) Use in production. Distillates...distilling system before the production gauge and promptly...the distilled spirits plant from which the...

2012-04-01

112

Distillation process using microchannel technology  

DOEpatents

The disclosed invention relates to a distillation process for separating two or more components having different volatilities from a liquid mixture containing the components. The process employs microchannel technology for effecting the distillation and is particularly suitable for conducting difficult separations, such as the separation of ethane from ethylene, wherein the individual components are characterized by having volatilities that are very close to one another.

Tonkovich, Anna Lee (Dublin, OH); Simmons, Wayne W. (Dublin, OH); Silva, Laura J. (Dublin, OH); Qiu, Dongming (Carbondale, IL); Perry, Steven T. (Galloway, OH); Yuschak, Thomas (Dublin, OH); Hickey, Thomas P. (Dublin, OH); Arora, Ravi (Dublin, OH); Smith, Amanda (Galloway, OH); Litt, Robert Dwayne (Westerville, OH); Neagle, Paul (Westerville, OH)

2009-11-03

113

Fractional distillation as a strategy for reducing the genotoxic potential of SRC-II coal liquids: a status report  

SciTech Connect

This report presents results of studies on the effects of fractional distillation on the genotoxic potential of Solvent Refined Coal (SRC-II) liquids. SRC-II source materials and distilled liquids were provided by Pittsburg and Midway Coal Mining Co. Fractional distillations were conducted on products from the P-99 process development unit operating under conditions approximating those anticipated at the SRC-II demonstration facility. Distillation cuts were subjected to chemical fractionation, in vitro bioassay and initial chemical analysis. Findings are discussed as they relate to the temperature at which various distillate cuts were produced. This document is the first of two status reports scheduled for 1981 describing these studies.

Pelroy, R.A.; Wilson, B.W.

1981-09-01

114

Vacuum mechatronics  

NASA Technical Reports Server (NTRS)

The discipline of vacuum mechatronics is defined as the design and development of vacuum-compatible computer-controlled mechanisms for manipulating, sensing and testing in a vacuum environment. The importance of vacuum mechatronics is growing with an increased application of vacuum in space studies and in manufacturing for material processing, medicine, microelectronics, emission studies, lyophylisation, freeze drying and packaging. The quickly developing field of vacuum mechatronics will also be the driving force for the realization of an advanced era of totally enclosed clean manufacturing cells. High technology manufacturing has increasingly demanding requirements for precision manipulation, in situ process monitoring and contamination-free environments. To remove the contamination problems associated with human workers, the tendency in many manufacturing processes is to move towards total automation. This will become a requirement in the near future for e.g., microelectronics manufacturing. Automation in ultra-clean manufacturing environments is evolving into the concept of self-contained and fully enclosed manufacturing. A Self Contained Automated Robotic Factory (SCARF) is being developed as a flexible research facility for totally enclosed manufacturing. The construction and successful operation of a SCARF will provide a novel, flexible, self-contained, clean, vacuum manufacturing environment. SCARF also requires very high reliability and intelligent control. The trends in vacuum mechatronics and some of the key research issues are reviewed.

Hackwood, Susan; Belinski, Steven E.; Beni, Gerardo

1989-01-01

115

Vacuum Energy  

E-print Network

There appears to be three, perhaps related, ways of approaching the nature of vacuum energy . The first is to say that it is just the lowest energy state of a given, usually quantum, system. The second is to equate vacuum energy with the Casimir energy. The third is to note that an energy difference from a complete vacuum might have some long range effect, typically this energy difference is interpreted as the cosmological constant. All three approaches are reviewed, with an emphasis on recent work. It is hoped that this review is comprehensive in scope. There is a discussion on whether there is a relation between vacuum energy and inertia. The solution suggested here to the nature of the vacuum is that Casimir energy can produce short range effects because of boundary conditions, but that at long range there is no overall effect of vacuum energy, unless one considers lagrangians of higher order than Einstein's as vacuum induced. No original calculations are presented in support of this position. This is not a review of the cosmological constant {\\it per se}, but rather vacuum energy in general, my approach to the cosmological constant is not standard.

Mark D. Roberts

2000-12-07

116

Vacuum Virtues  

ERIC Educational Resources Information Center

Upright vacuums, like cars, vary in quality, features and performance. Like automobiles, some uprights are reliable, others may be problematic, and some become a problem as a result of neglect or improper use. So, how do education institutions make an informed choice and, having done so, ensure that an upright vacuum goes the distance? In this…

Rathey, Allen

2007-01-01

117

European refinery utilization: Consider the combined effects of distillation and conversion  

SciTech Connect

Despite a weaker relationship between capacity utilization and complex refining margins in Europe, a correlation with distillation margins remains. Distillation capacity utilization has historically been correlated with overall complex refining margins. However, in recent years that relationship has become more tenuous. The main reason appears to be that utilization rates in secondary processing units, including conversion units, have declined and eroded conversion margins. This has been difficult for the outside observer to monitor because of the lack of comprehensive and timely data on secondary utilization rates. A second factor may have been underestimation of installed capacity due to modifications since installation. Nevertheless, the relationship between distillation capacity utilization and distillation margins has remained a good one. Consequently, there may be considerable value in forecasting utilization rates so that it is possible to assess the outlook for distillation margins.

Hudson, J.M.; Gray, G.M. [Salmon Brothers, London (United Kingdom)

1996-01-01

118

Gravitational vacuum  

NASA Astrophysics Data System (ADS)

The existence of a special gravitational vacuum is considered in this paper. A phenomenological method differing from the traditional Einsteinian formalization is utilized. Vacuum, metric and matter form a complex determined by field equations and at great distances from gravitational masses vacuum effects are small but could be large in powerful fields. Singularities and black holes justify the approach as well as the Ambartsmyan theory concerning the existence of supermassive and superdense prestallar bodies that then disintegrate. A theory for these superdense bodies is developed involving gravitational field equations that describe the vacuum by an energy momentum tensor and define the field and mass distribution. Computations based on the theory for gravitational radii with incompressible liquid models adequately reflecting real conditions indicate that a gravitational vacuum could have considerable effects on superdense stars and could have radical effects for very large masses.

Grigoryan, L. S.; Saakyan, G. S.

1984-09-01

119

Antioxidant Activity of Phytochemicals from Dried Distillers Grain Oil  

Technology Transfer Automated Retrieval System (TEKTRAN)

A distillate was obtained by molecular distillation of oil extracted from distiller’s dried grains (DDG). The dried distiller’s grains distillate (DDGD) contained phytosterols, steryl ferulates, tocopherols, tocotrienols, and carotenoids. DDGD was tested for its impact on the oxidative stability i...

120

Antioxidant activity of phytochemicals from dried distillers grain oil  

Technology Transfer Automated Retrieval System (TEKTRAN)

A distillate was obtained by molecular distillation of oil extracted from distiller’s dried grains (DDG). The dried distiller’s grains distillate (DDGD) contained phytosterols, steryl ferulates, tocopherols, tocotrienols, and carotenoids. DDGD was tested for its impact on the oxidative stability in...

121

On the evolution of morphology of zirconium sponge during reduction and distillation  

SciTech Connect

High purity zirconium metal is produced by magnesio-thermic reduction of zirconium tetrachloride followed by vacuum distillation. The reduction process is carried out in a batch giving metal sponge and magnesium chloride in the reduced mass. The sponge is purified to using by vacuum distillation. The morphology of the sponge formed during the reduction and its influence on further processing has significant importance. In the present study, a detailed investigation involving evolution of the morphology of sponge particles and its implication during the vacuum distillation was carried out. The study of the microstructure was done using scanning electron microscopy and X-ray diffraction. It is observed that the nascent sponge formed is highly unstable which transforms to a needle-like morphology almost immediately, which further transforms to rounded and finally to a bulk shape. Faceting of the surface and needle-shape formation were observed in these particles, this is probably due to anisotropy in the surface energy. The morphology of the sponge formed during the reduction influences the distillation process. The fine needle-like shape sponge morphology leads to particle ejection, which is explained to be due to curvature effect. This is responsible for the formation of unwanted mass during distillation. XRD line broadening analysis indicates that the individual sponge particles are free from structural defects (dislocation) and are nearly single crystalline in nature.

Kapoor, K. [Nuclear Fuel Complex, Hyderabad, 500 062 (India)], E-mail: kapoork@nfc.ernet.in; Padmaprabu, C.; Nandi, D. [Nuclear Fuel Complex, Hyderabad, 500 062 (India)

2008-03-15

122

Distillation Apparatuses Using Household Items  

NASA Astrophysics Data System (ADS)

A simple apparatus to demonstrate distillation principles can be very difficult to build without the specialty glassware found in chemistry laboratories. We have built inexpensive but effective distillation apparatuses from equipment that can be easily purchased at local department, grocery, or hardware stores. In one apparatus, colored water is heated to boiling and the condensed vapors drip into another container. In another apparatus, acetone is heated to boiling with hot water and the acetone vapors condense onto a Styrofoam cup. The Styrofoam cup is softened by the acetone and collapses. Rubbing alcohol can be used instead of acetone, but the cup is not softened and the boiling point is much higher. Both apparatuses can be used in a classroom. Both are simple, cost-effective ways of demonstrating distillation, evaporation, and condensation. They would be ideal to use in elementary and middle school classrooms when explaining these concepts.

Campanizzi, Danielle R. D.; Mason, Brenda; Hermann, Christine K. F.

1999-08-01

123

Better vacuum by removal of diffusion-pump-oil contaminants  

NASA Technical Reports Server (NTRS)

The complex problem of why large space simulation chambers do not realize true ultimate vacuum was investigated. Some contaminating factors affecting diffusion pump performance were identified, and some advances in vacuum distillation-fractionation technology were achieved which resulted in a two-decade-or-more lower ultimate pressure. Data are presented to show the overall or individual contaminating effects of commonly used phthalate ester plasticizers of 390 to 530 molecular weight on diffusion pump performance. Methods for removing contaminants from diffusion pump silicone oil during operation and for reclaiming contaminated oil by high-vacuum molecular distillation are described. Conceptual self-cleansing designs and operating procedures are proposed for modifying large diffusion pumps into high-efficiency distillation devices. The potential exists for application of these technological advancements to other disciplines, such as medicine, biomedical materials, metallurgy, refining, and chemical (diffusion-enrichment) processing.

Buggele, A. E.

1975-01-01

124

Energy Recovery in Industrial Distillation Processes  

E-print Network

ENERGY RECOVERY IN INDUSTRIAL DISTILLATION PROCESSES Duane B. Paul General Electric Company Fitchburg, Massachusetts ABSTRACT Overhead separati on processes whi ch present attracti ve Distillation processes are energy intensive Condenser...

Paul, D. B.

1983-01-01

125

Properties of Distillers Grains Composites  

Technology Transfer Automated Retrieval System (TEKTRAN)

Interest in renewable biofuel sources has intensified in recent years, leading to greatly increased production of ethanol and its primary coproduct, Distillers Dried Grain with Solubles (DDGS). Consequently, the development of new outlets for DDGS has become crucial to maintaining the economic viab...

126

Optimal Control of Distillation Systems  

E-print Network

is therefore the first requirement of optimal control. Use of Slip-Stream Consider the distillation of a binary mixture where one or both components are valuable. are required pure, and are separated in a single column. The objective is to obtain maximum...

Chatterjee, N.; Suchdeo, S. R.

1984-01-01

127

Corrosion inhibition for distillation apparatus  

DOEpatents

Tower material corrosion in an atmospheric or sub-atmospheric distillation tower in a coal liquefaction process is reduced or eliminated by subjecting chloride-containing tray contents to an appropriate ion-exchange resin to remove chloride from such tray contents materials.

Baumert, Kenneth L. (Emmaus, PA); Sagues, Alberto A. (Lexington, KY); Davis, Burtron H. (Georgetown, KY); Schweighardt, Frank K. (Upper Macungie, PA)

1985-01-01

128

Contextual Reasoning Distilled M. Benerecetti  

E-print Network

Contextual Reasoning Distilled M. Benerecetti , P. Bouquet , and C. Ghidini ¡ ¢ Dip. di Chester Street, Manchester M1 5GD, U.K. Phone number: +44 (0)161 247 1556 C.Ghidini@doc.mmu.ac.uk Abstract can be traced back to R. Weyhrauch and his work on mechanising logical theories in the interactive

Bouquet, Paolo

129

27 CFR 19.322 - Distillates containing extraneous substances.  

Code of Federal Regulations, 2010 CFR

... DISTILLED SPIRITS PLANTS Production § 19.322 Distillates...system prior to the production gauge for addition...the distilled spirits plant from which the distillates...spirits for use in wine production and the receipt...

2010-04-01

130

27 CFR 1.91 - Bottled distilled spirits.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Bottled distilled spirits. 1.91 Section 1.91 Alcohol...ADMINISTRATION ACT, NONINDUSTRIAL USE OF DISTILLED SPIRITS AND WINE, BULK SALES AND BOTTLING OF DISTILLED SPIRITS Bulk Sales and Bottling of Distilled...

2010-04-01

131

21 CFR 184.1848 - Starter distillate.  

Code of Federal Regulations, 2011 CFR

...Starter distillate (butter starter distillate) is a steam distillate of the culture of any or all of the following species of bacteria grown on a medium consisting of skim milk usually fortified with about 0.1 percent citric acid: Streptococcus...

2011-04-01

132

Oil recovery from condensed corn distillers solubles  

Microsoft Academic Search

Condensed corn distillers solubles (CCDS) contains more oil than dried distillers grains with solubles (DDGS), 20 vs. 12% (dry weight basis). Therefore, significant amount of oil is present in the liquid fraction after fermentation and ethanol distillation. The oil removed represents a significant alternative feedstock for biodiesel production. The objectives of the present research were to study the effect of

Sandra Majoni

2009-01-01

133

Intermediate Vapor Expansion Distillation and Nested Enrichment Cascade Distillation  

E-print Network

is described in three configurations overhead vapor compresed, bottoms vapor compressed, or completely closed cycle. As with conventional cascades, conventional heat pumping does to increase the distillation efficiency. Heat pumping merely substitutes...) from overhead to interreboiler; 2) from intercondenser to bottoms reboilerj or 3) from intercondenser to interreboiler. Also, the vapor being compressed can be overhead vapor, bottoms vapor, or a separate closed cycle vapor. Thus there are nine...

Erickson, D. C.

134

Fate of pesticides in a distilled spirit of barley shochu during the distillation process.  

PubMed

Moromi (the fermented mash) of "mugi shochu" that had been artificially contaminated with pesticides was distilled to elucidate the fate of pesticides in the distillation process. The pesticides residing in the distillate were quantified by liquid chromatography-tandem mass spectrometry (LC-MS/MS). Of the analyzed pesticides (249 compounds), 89% were not detected in the distillate, showing that the distillation process minimized the risk of pesticide contamination. PMID:21150108

Inoue, Tomonori; Nagatomi, Yasushi; Kinami, Tomohisa; Uyama, Atsuo; Mochizuki, Naoki

2010-01-01

135

The fate of mycotoxins during the distillation process of barley shochu, a distilled alcoholic beverage.  

PubMed

Mycotoxins are frequent contaminants of grains and critical risk substances for brewers. Fermented barley mash contaminated artificially with 13 representative mycotoxins was distilled with small-scale apparatuses to elucidate the possibility of mycotoxin transfer from mash to distillates. None of these were detected in the distillates. The distillation process can effectively reduce the contamination risk posed by mycotoxins in distilled alcoholic beverages. PMID:22232264

Nagatomi, Yasushi; Inoue, Tomonori; Uyama, Atsuo; Mochizuki, Naoki

2012-01-01

136

Distillation and Air Stripping Designs for the Lunar Surface  

NASA Technical Reports Server (NTRS)

Air stripping and distillation are two different gravity-based methods, which may be applied to the purification of wastewater on the lunar base. These gravity-based solutions to water processing are robust physical separation techniques, which may be advantageous to many other techniques for their simplicity in design and operation. The two techniques can be used in conjunction with each other to obtain high purity water. The components and feed compositions for modeling waste water streams are presented in conjunction with the Aspen property system for traditional stage distillation models and air stripping models. While the individual components for each of the waste streams will vary naturally within certain bounds, an analog model for waste water processing is suggested based on typical concentration ranges for these components. Target purity levels for the for recycled water are determined for each individual component based on NASA s required maximum contaminant levels for potable water Distillation processes are modeled separately and in tandem with air stripping to demonstrate the potential effectiveness and utility of these methods in recycling wastewater on the Moon. Optimum parameters such as reflux ratio, feed stage location, and processing rates are determined with respect to the power consumption of the process. Multistage distillation is evaluated for components in wastewater to determine the minimum number of stages necessary for each of 65 components in humidity condensate and urine wastewater mixed streams. Components of the wastewater streams are ranked by Henry s Law Constant and the suitability of air stripping in the purification of wastewater in terms of component removal is evaluated. Scaling factors for distillation and air stripping columns are presented to account for the difference in the lunar gravitation environment. Commercially available distillation and air stripping units which are considered suitable for Exploration Life Support are presented. The advantages to the various designs are summarized with respect to water purity levels, power consumption, and processing rates.

Boul, Peter J.; Lange, Kevin E.; Conger, Bruce; Anderson, Molly

2009-01-01

137

Vacuum Gauges  

NSDL National Science Digital Library

This is a description for a learning module from Maricopa Advanced Technology Education Center. This PDF describes the module; access may be purchased by visiting the MATEC website. Semiconductor manufacturing equipment requires the use of many different types of vacuum gauges. Selection is based on range of process operations and production requirements. This MATEC module explores the theory and functionality of vacuum gauges and provides many examples of different types of gauges. The focus is on understanding the operating ranges and application constraints of each type of gauge. Mathematical equations are used to explain calibration, sensitivity, and overall operations of each type of gauge.

2012-11-28

138

Toxicity and toxicokinetics of binary combinations of petroleum hydrocarbon distillates with the earthworm Eisenia andrei.  

PubMed

Petroleum hydrocarbons (PHCs) act via narcosis and are expected to have additive toxicity. However, previous work has demonstrated less-than-additive toxicity with PHC distillates and earthworms. A study was initiated to investigate this through toxicity and toxicokinetic studies with the earthworm Eisenia andrei. Three petroleum distillate fractions, F2 (>C10-C16), F3a (>C16-C23), and F3b (>C23-C34), were used in two binary combinations, F2F3a and F3aF3b. In the toxicity study, clean soil was spiked with equitoxic combinations of the two distillates ranging from 0.5 to 2.5 toxic units. In the toxicokinetic study, a binary combination consisting of one concentration of each distillate was used. On a soil concentration basis, the toxicity of the binary combinations of distillates was less than additive. Accumulation of the individual distillates, however, was generally reduced when a second distillate was present, resulting in lower body burden. This is thought to be due to the presence of a nonaqueous-phase liquid at the soil concentrations used. On a tissue concentration basis, toxicity was closer to additive. The results demonstrate that tissue concentrations are the preferred metric for toxicity for earthworms. They also demonstrate that the Canada-wide soil standards based on individual distillates are likely protective. PMID:23401139

Cermak, Janet; Stephenson, Gladys; Birkholz, Detlef; Dixon, D George

2013-04-01

139

Free Boundary Problems in Distillation.  

NASA Astrophysics Data System (ADS)

Design and scaleup of distillation equipment requires an understanding of the vapor-liquid equilibria as well as an understanding of the column hydraulics. This work focuses on two problems of fluid mechanics important in understanding the behavior of distillation columns: the shapes and stability of dielectric drops in an electric field and the flow patterns on distillation trays. Axisymmetric equilibrium shapes and stability of dielectric drops subject to an applied electric field are determined by solving simultaneously the Young-Laplace equation for drop shape and the Maxwell equations for field distribution. Both linearly and nonlinearly polarizable drops are studied, as are drops that are pendant/sessile on a supporting plate and those that are floating freely between two plates. The range of parameters for which hysteresis in drop deformation can be observed is given for linearly and nonlinearly polarizable drops. Properly accounting for the effects of nonlinear polarization brings the theoretical results of this work into accord with previously published experimental results. Detailed examination of the electric fields inside nonlinearly polarizable drops reveals that they are very nonuniform, in contrast to the nearly uniform fields usually found in linearly polarizable drops. The concept of depth averaging the equations of motion for a thin film (relative to the length of the distillation tray) is used to reduce the three-dimensional, free surface flow problem to two dimensions. A one-dimensional model is first used to gain understanding into the behavior of the bulk flow, ignoring any edge effects. A rise in the height profile on the tray, or hydraulic jump, is predicted. The effects of Reynolds number, capillary number (surface tension), tray geometry, and film thickness are all examined. The importance of the downcomers is shown. The two-dimensional model allows examination not only of rectangular trays, but also round trays and trays which are annular arcs, so called "race track" trays. A large zone of recirculation is predicted near the walls of round trays. This is confirmed in published experimental results and in experimental observations reported here. Race track trays did not show recirculation even at large arc angles.

Wohlhuter, Frederick Karl

140

Vapor Compression Distillation Flight Experiment  

NASA Technical Reports Server (NTRS)

One of the major requirements associated with operating the International Space Station is the transportation -- space shuttle and Russian Progress spacecraft launches - necessary to re-supply station crews with food and water. The Vapor Compression Distillation (VCD) Flight Experiment, managed by NASA's Marshall Space Flight Center in Huntsville, Ala., is a full-scale demonstration of technology being developed to recycle crewmember urine and wastewater aboard the International Space Station and thereby reduce the amount of water that must be re-supplied. Based on results of the VCD Flight Experiment, an operational urine processor will be installed in Node 3 of the space station in 2005.

Hutchens, Cindy F.

2002-01-01

141

Vacuum pyrolysis of used tires  

SciTech Connect

The vacuum pyrolysis of used tires enables the recovery of useful products, such as pyrolytic oil and pyrolytic carbon black (CB{sub P}). The light part of the pyrolytic oil contains dl-limonene which has a high price on the market. The naphtha fraction can be used as a high octane number component for gasoline. The middle distillate demonstrated mechanical and lubricating properties similar to those of the commercial aromatic oil Dutrex R 729. The heavy oil was tested as a feedstock for the production of needle coke. It was found that the surface morphology of CB{sub P} produced by vacuum pyrolysis resembles that of commercial carbon black. The CB{sub P} contains a higher concentration of inorganic compounds (especially ZnO and S) than commercial carbon black. The pyrolysis process feasibility looks promising. One old tire can generate upon vacuum pyrolysis, incomes of at least $2.25 US with a potential of up to $4.83 US/tire upon further product improvement. The process has been licensed to McDermott Marketing Servicing Inc. (Houston) for its exploitation in the US.

Roy, C.; Darmstadt, H.; Benallal, B.; Chaala, A.; Schwerdtfeger, A.E. [Univ. Laval, Quebec City, Quebec (Canada). Dept. de Geneie Chimique

1995-11-01

142

Potential bleaching techniques for corn distillers grains  

Technology Transfer Automated Retrieval System (TEKTRAN)

The ethanol industry is booming, and extensive research is now being pursued to develop alternative uses for distillers dried grains (DDG) and distillers dried grains with solubles (DDGS), coproducts of the ethanol production process. Currently, DDG and DDGS are used exclusively as livestock feed. P...

143

Recycling of Waste Acetone by Fractional Distillation  

ERIC Educational Resources Information Center

Distillation is a ubiquitous technique in the undergraduate organic chemistry curriculum; the technique dates back to ca. 3500 B.C.E. With the emergence of green chemistry in the 1990s, the importance of emphasizing responsible waste management practices for future scientists is paramount. Combining the practice of distillation with the message…

Weires, Nicholas A.; Johnston, Aubrey; Warner, Don L.; McCormick, Michael M.; Hammond, Karen; McDougal, Owen M.

2011-01-01

144

Chemical and biological effects of heavy distillate recycle in the SRC-II process  

SciTech Connect

Recent work from the Merriam Laboratory continuous coal liquefaction units shows that heavy distillate from the SRC-II process can be recycled to extinction, and hence a distillate product boiling entirely below 310/sup 0/C (590/sup 0/F) (or other selected boiling points) is feasible. In these runs distillate yield was not reduced; gas make was unaffected; and hydrogen consumption was increased only slightly, in keeping with the generally higher hydrogen content of lighter end products. Total distillate yield (C/sub 5/-590/sup 0/F) was 56 wt %, MAF coal in runs with subbituminous coal from the Amax Belle Ayr mine. Product endpoint is well below 371/sup 0/C (700/sup 0/F), the temperature above which coal distillates appear to become genotoxic; and the product was shown to be free of mutagenic activity in the Ames test. Chemical analyses showed both the < 270/sup 0/C (< 518/sup 0/F) and the < 310/sup 0/C (< 590/sup 0/F) distillates to be essentially devoid of several reference polycyclic compounds known to be carcinogenic in laboratory animals. Tests for tumorigenic or carcinogenic activity were not carried out on these materials. However, a comparison of chemical data from the Merriam heavy distillate samples with data on the other SRC-II distillates where carcinogenesis or tumorigenesis data is available leads to the expectation that < 371/sup 0/C (< 700/sup 0/F) materials from the Merriam Laboratory will have greatly reduced tumorigenic and carcinogenic activity in skin painting tests. Other studies suggest the product should be more readily upgraded than full-range (C/sub 5/-900/sup 0/F) distillate.

Wilson, B.W.; Pelroy, R.A.; Anderson, R.P.; Freel, J.

1983-12-01

145

27 CFR 19.65 - Experimental distilled spirits plants.  

Code of Federal Regulations, 2010 CFR

...false Experimental distilled spirits plants. 19.65 Section 19.65 Alcohol...TREASURY LIQUORS DISTILLED SPIRITS PLANTS Administrative and Miscellaneous Provisions...65 Experimental distilled spirits plants. The appropriate TTB officer may...

2010-04-01

146

27 CFR 19.32 - Experimental distilled spirits plants.  

Code of Federal Regulations, 2011 CFR

...false Experimental distilled spirits plants. 19.32 Section 19.32 Alcohol...TREASURY LIQUORS DISTILLED SPIRITS PLANTS Administrative and Miscellaneous Provisions...32 Experimental distilled spirits plants. (a) General. The...

2011-04-01

147

40 CFR 721.9635 - Terpene residue distillates.  

Code of Federal Regulations, 2010 CFR

...2010-07-01 2010-07-01 false Terpene residue distillates. 721.9635 Section...Specific Chemical Substances § 721.9635 Terpene residue distillates. (a) Chemical...chemical substance identified generically as terpene residue distillates (PMN...

2010-07-01

148

7 CFR 160.8 - Steam distilled wood turpentine.  

Code of Federal Regulations, 2010 CFR

... 2010-01-01 false Steam distilled wood turpentine. 160.8 Section 160.8 ...STORES General § 160.8 Steam distilled wood turpentine. The designation “steam distilled wood turpentine” shall refer to the kind...

2010-01-01

149

7 CFR 160.9 - Destructively distilled wood turpentine.  

Code of Federal Regulations, 2010 CFR

...2010-01-01 false Destructively distilled wood turpentine. 160.9 Section 160.9...General § 160.9 Destructively distilled wood turpentine. The designation “destructively distilled wood turpentine” shall refer to the kind...

2010-01-01

150

7 CFR 160.9 - Destructively distilled wood turpentine.  

Code of Federal Regulations, 2013 CFR

...2013-01-01 false Destructively distilled wood turpentine. 160.9 Section 160.9...General § 160.9 Destructively distilled wood turpentine. The designation “destructively distilled wood turpentine” shall refer to the kind...

2013-01-01

151

7 CFR 160.8 - Steam distilled wood turpentine.  

Code of Federal Regulations, 2013 CFR

... 2013-01-01 false Steam distilled wood turpentine. 160.8 Section 160.8 ...STORES General § 160.8 Steam distilled wood turpentine. The designation “steam distilled wood turpentine” shall refer to the kind...

2013-01-01

152

7 CFR 160.9 - Destructively distilled wood turpentine.  

...2014-01-01 false Destructively distilled wood turpentine. 160.9 Section 160.9...General § 160.9 Destructively distilled wood turpentine. The designation “destructively distilled wood turpentine” shall refer to the kind...

2014-01-01

153

7 CFR 160.9 - Destructively distilled wood turpentine.  

Code of Federal Regulations, 2011 CFR

...2011-01-01 false Destructively distilled wood turpentine. 160.9 Section 160.9...General § 160.9 Destructively distilled wood turpentine. The designation “destructively distilled wood turpentine” shall refer to the kind...

2011-01-01

154

7 CFR 160.8 - Steam distilled wood turpentine.  

Code of Federal Regulations, 2012 CFR

... 2012-01-01 false Steam distilled wood turpentine. 160.8 Section 160.8 ...STORES General § 160.8 Steam distilled wood turpentine. The designation “steam distilled wood turpentine” shall refer to the kind...

2012-01-01

155

7 CFR 160.8 - Steam distilled wood turpentine.  

... 2014-01-01 false Steam distilled wood turpentine. 160.8 Section 160.8 ...STORES General § 160.8 Steam distilled wood turpentine. The designation “steam distilled wood turpentine” shall refer to the kind...

2014-01-01

156

7 CFR 160.9 - Destructively distilled wood turpentine.  

Code of Federal Regulations, 2012 CFR

...2012-01-01 false Destructively distilled wood turpentine. 160.9 Section 160.9...General § 160.9 Destructively distilled wood turpentine. The designation “destructively distilled wood turpentine” shall refer to the kind...

2012-01-01

157

7 CFR 160.8 - Steam distilled wood turpentine.  

Code of Federal Regulations, 2011 CFR

... 2011-01-01 false Steam distilled wood turpentine. 160.8 Section 160.8 ...STORES General § 160.8 Steam distilled wood turpentine. The designation “steam distilled wood turpentine” shall refer to the kind...

2011-01-01

158

27 CFR 19.32 - Experimental distilled spirits plants.  

...false Experimental distilled spirits plants. 19.32 Section 19.32 Alcohol...TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Administrative and Miscellaneous Provisions...32 Experimental distilled spirits plants. (a) General. The...

2014-04-01

159

Combined distillation and normal freezing to purify elements of groups II and VI  

NASA Technical Reports Server (NTRS)

A practical system and its application to the purification of Te and Cd is described. Single crystals are grown directly in vitreous silica ampoules subsequently used for sealed Bridgman growth of (Hg-Cd)Te. The system also prepares the ampoules by heating in high vacuum. Purification of the elements is by the combined effect of distillation and normal freezing. Transport and segregation are discussed.

Holland, L. R.

1984-01-01

160

Shell middle distillate hydrogenation process  

SciTech Connect

The strive towards cleaner environment has lead to low sulfur specifications for middle distillate fuels. In addition compositional specifications are presently debated. Thus, to meet future emissions standards regarding, specifically, particulates emissions, the motor industry calls for improved automotive gasoil quality. Although automotive gasoil quality affects emissions from diesel engines it is considered less influential than engine design and maintenance. Sulfur, density and cetane number are the fuel properties having the greatest influence on diesel engine emissions although also aromatics and endpoint specifications have been defined in environmentally adopted government initiatives. This paper reviews the options which are available to tackle these new requirements. The high severity single stage concept (using conventional mixed sulfides catalysts) will be discussed in its potential to meet more severe product requirements as well as in terms of its limitations, especially at the point of aromatics saturation and cetaine upgrading. Furthermore, it is shown that the option of severe hydrotreating followed by hydrogenation with conventional noble metal catalysts is preferred if deep aromatics saturation is aimed at. However, this conventional two stage concept has limitations with respect to heaviness and sulfur and nitrogen content of feedstocks. The new Shell Middle Distillate Hydrogenation (SMDH) technology, applying a (semi) two stage approach based on the Shell developed hydrogenation catalyst is presented. The SMDH process will be discussed in its potential to break the limitations of the conventional options. The new catalyst is crucial in this process and allows a highly integrated mode of operation. A number of applications of this novel process will be discussed.

Lucien, J.P. [Companie Rhenane de Raffinage Reichstett, Reichstett Vendenheim (France); Berg, J.P. van den; Hooijdonk, H.M.J.H. van; Thielemans, G.L.B. [Shell Internationale Petroleum Mij., The Hague (Netherlands); Germaine, G. [Shell Recherche SA, Grand-Couronne (France); Gjers, M. [Shell Raffinaderi AB, Gothenburg (Sweden)

1994-12-31

161

Applying risk assessment principles to a batch distillation column  

SciTech Connect

Some distillation columns in the chemical industry are operated in batch mode with a fairly short operating cycle. At the end of each cycle the columns are cooled and recharged. During the cooling cycle, air will be drawn into the column by the action of a vacuum relief valve. Consequently, for a finite portion of the operating cycle a flammable mixture will exist in the column. Here we evaluate the risk posed by such an operation to see if a mitigation measure is justified. We develop a fault tree and estimate the frequency of ignition by all possible ignition sources. By comparing the risk reduction attainable by installing a lightning protection system with that attainable by using an inert blanketing system the lightning protection system is found to be the preferred solution. It provides about the same risk reduction at a lower overall cost. 2 refs., 3 figs., 4 tabs.

Woodward, J.L.; Moosemiller, M.D. [DNV Technica, Columbus, OH (United States)] [DNV Technica, Columbus, OH (United States)

1996-12-31

162

An improved model for multiple effect distillation  

E-print Network

Increasing global demand for fresh water is driving research and development of advanced desalination technologies. As a result, a detailed model of multiple effect distillation (MED) is developed that is flexible, simple ...

Mistry, Karan H.

163

Minimizing corrosion in coal liquid distillation  

DOEpatents

In an atmospheric distillation tower of a coal liquefaction process, tower materials corrosion is reduced or eliminated by introduction of boiling point differentiated streams to boiling point differentiated tower regions.

Baumert, Kenneth L. (Emmaus, PA); Sagues, Alberto A. (Lexington, KY); Davis, Burtron H. (Georgetown, KY)

1985-01-01

164

Development of energy efficient membrane distillation systems  

E-print Network

Membrane distillation (MD) has shown potential as a means of desalination and water purification. As a thermally driven membrane technology which runs at relatively low pressure, which can withstand high salinity feed ...

Summers, Edward K

2013-01-01

165

Pilot-scale distillation and characterization of diesel-fuel fractions of Strategic Petroleum Reserve crude oils. Interim report, December 1985February 1987  

Microsoft Academic Search

Little, beyond crude assay data, has been known about the properties of various fuel fractions, including diesel fuel, that might ensue in the event crude oils available at the Strategic Petroleum Reserve were actually to be refined. Accordingly, eight distinct crude-oil streams were collected from the Reserve and subjected to distillation in a pilot-scale unit. Middle distillate fractions were prepared

D. L. Morris; B. K. Bailey; L. L. Stavinoha; H. N. Giles

1987-01-01

166

COED Transactions, Vol. X, No. 5, May 1978. STAGEF, A Program to Compute the Internal Variables of an Operating Distillation Column.  

ERIC Educational Resources Information Center

A digital computer program, STAGEF, designed for use with the distillation experiments in a typical undergraduate Chemical Engineering laboratory in Unit Operations is explained. The program enables the student to determine the rate of liquid overflow and vapor boil-up which leaves each tray within the distillation column. The student may also…

Marcovitz, Alan B., Ed.

167

Reducing Energy Usage in Extractive Distillation  

E-print Network

, .. ~ REDUCING ENERGY USAGE IN,EXTRACTIVE DISTILLATION A. C. Saxena V. A. Bhandari Polysar Limited Sarnia, Ontario, Canada Abstract Butadiene 1:3 is separated from other C. hydrocarbons by extractive distillation in a sieve plate tower... not affect tower stability and the operators h~,e adapted well to the new control strategy. INTRODUCTION For its rubber manufacturing operations at Sarnia, Ontario, Canada, Polysar Limited extracts butadiene 1:3 from a mixed C. hydrocarbon feed...

Saxena, A. C.; Bhandari, V. A.

168

Multipartite secret key distillation and bound entanglement  

SciTech Connect

Recently it has been shown that quantum cryptography beyond pure entanglement distillation is possible and a paradigm for the associated protocols has been established. Here we systematically generalize the whole paradigm to the multipartite scenario. We provide constructions of new classes of multipartite bound entangled states, i.e., those with underlying twisted Greenberger-Horne-Zeilinger (GHZ) structure and nonzero distillable cryptographic key. We quantitatively estimate the key from below with the help of the privacy squeezing technique.

Augusiak, Remigiusz; Horodecki, Pawel [Faculty of Applied Physics and Mathematics, Gdansk University of Technology, Narutowicza 11/12, 80-952 Gdansk (Poland) and ICFO-Institute Ciencies Fotoniques, Mediterranean Technology Park, 08860 Castelldefels (Barcelona) (Spain); Faculty of Applied Physics and Mathematics, Gdansk University of Technology, Narutowicza 11/12, 80-952 Gdansk (Poland)

2009-10-15

169

Distillation tray structural parameter study: Phase 1  

NASA Technical Reports Server (NTRS)

The purpose here is to identify the structural parameters (plate thickness, liquid level, beam size, number of beams, tray diameter, etc.) that affect the structural integrity of distillation trays in distillation columns. Once the sensitivity of the trays' dynamic response to these parameters has been established, the designer will be able to use this information to prepare more accurate specifications for the construction of new trays. Information is given on both static and dynamic analysis, modal response, and tray failure details.

Winter, J. Ronald

1991-01-01

170

27 CFR 17.162 - Receipt of distilled spirits.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Receipt of distilled spirits. 17.162 Section 17.162 Alcohol...LIQUORS DRAWBACK ON TAXPAID DISTILLED SPIRITS USED IN MANUFACTURING NONBEVERAGE PRODUCTS...Records § 17.162 Receipt of distilled spirits. (a) Distilled spirits...

2010-04-01

171

27 CFR 1.90 - Distilled spirits in bulk.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 2010-04-01 false Distilled spirits in bulk. 1.90 Section 1.90 Alcohol...ADMINISTRATION ACT, NONINDUSTRIAL USE OF DISTILLED SPIRITS AND WINE, BULK SALES AND BOTTLING OF DISTILLED SPIRITS Bulk Sales and Bottling of Distilled...

2010-04-01

172

CHEM333: Lab Experiment 3: Distillation and Gas Chromatography  

E-print Network

CHEM­333: Lab Experiment 3: Distillation and Gas Chromatography: Prelab-Assignment: read Chapters 5 and evaluate the efficiency of the fractional distillation versus simple distillation by gas chromatography discussion of gas chromatography. For your distillations (remember to add boiling stones) you will use 30 m

Taber, Douglass

173

Quantum Nonlocal Boxes Exhibit Stronger Distillability  

NASA Astrophysics Data System (ADS)

The hypothetical nonlocal box (NLB) proposed by Popescu and Rohrlich allows two spatially separated parties, Alice and Bob, to exhibit stronger than quantum correlations. If the generated correlations are weak, they can sometimes be distilled into a stronger correlation by repeated applications of the NLB. Motivated by the limited distillability of NLBs, we initiate here a study of the distillation of correlations for nonlocal boxes that output quantum states rather than classical bits (qNLBs). We propose a new protocol for distillation and show that it asymptotically distills a class of correlated quantum nonlocal boxes to the value (1)/(2)(3? {3}+1) ? 3.098076, whereas in contrast, the optimal non-adaptive parity protocol for classical nonlocal boxes asymptotically distills only to the value 3.0. We show that our protocol is an optimal non-adaptive protocol for 1, 2 and 3 qNLB copies by constructing a matching dual solution for the associated primal semidefinite program (SDP). We conclude that qNLBs are a stronger resource for nonlocality than NLBs. The main premise that develops from this conclusion is that the NLB model is not the strongest resource to investigate the fundamental principles that limit quantum nonlocality. As such, our work provides strong motivation to reconsider the status quo of the principles that are known to limit nonlocal correlations under the framework of qNLBs rather than NLBs.

Høyer, Peter; Rashid, Jibran

2013-06-01

174

Antioxidant Activity of Phytochemicals from Distillers Dried Grain Oil  

Microsoft Academic Search

A distillate was obtained by molecular distillation of oil extracted from distillers dried grains (DDG). The distillers dried\\u000a grain oil distillate (DDGD) contained phytosterols, steryl ferulates, tocopherols, tocotrienols, and carotenoids. DDGD was\\u000a tested for its impact on the oxidative stability index (OSI) at 110 °C of soybean, sunflower, and high-oleic sunflower oils,\\u000a as well as the same oils that were stripped

Jill Kristine Winkler-Moser; Steven Francis Vaughn

2009-01-01

175

Utilization of wet distillers grains in high-energy beef cattle diets based on processed grain  

Technology Transfer Automated Retrieval System (TEKTRAN)

Distiller's grains (DG) are used extensively by beef cattle feeding operations in the United States, including the Southern Great Plains. Our regional research consortium has been conducting research focused on utilization of wet DG in feedlot diets based on steam-flaked corn (SFC). Effects of DG on...

176

75 FR 11147 - Notice of Intent To Grant Exclusive Patent License; Distilled Solutions, LLC  

Federal Register 2010, 2011, 2012, 2013

...in the United States, the Government- owned invention described in U.S. Patent No. 6,893,540, entitled ``High Temperature Peltier Effect Water Distiller,'' issued May 17, 2005, Navy Case No. 82,363. DATES: Anyone wishing to object...

2010-03-10

177

Vacuum Evaporation Technology for Treating Antimony-Rich Anode Slime  

NASA Astrophysics Data System (ADS)

A vacuum evaporation technology for treating antimony-rich anode slime was developed in this work. Experiments were carried out at temperatures from 873 K to 1073 K and residual gas pressures from 50 Pa to 600 Pa. During vacuum evaporation, silver from the antimony-rich anode slime was left behind in the distilland in a silver alloy containing antimony and lead, and antimony trioxide was evaporated. The experimental results showed that 92% by weight of antimony can be removed, and the silver content in the alloy was up to 12.84%. The antimony trioxide content in the distillate was more than 99.7%, and the distillate can be used directly as zero-grade antimony trioxide (China standard).

Qiu, Keqiang; Lin, Deqiang; Yang, Xuelin

2012-11-01

178

Design and the parametric testing of the space station prototype integrated vapor compression distillation water recovery module  

NASA Technical Reports Server (NTRS)

Potable water for the Space Station Prototype life support system is generated by the vapor compression technique of vacuum distillation. A description of a complete three-man modular vapor compression water renovation loop that was built and tested is presented; included are all of the pumps, tankage, chemical post-treatment, instrumentation, and controls necessary to make the loop representative of an automatic, self-monitoring, null gravity system. The design rationale is given and the evolved configuration is described. Presented next are the results of an extensive parametric test during which distilled water was generated from urine and urinal flush water with concentration of solids in the evaporating liquid increasing progressively to 60 percent. Water quality, quantity and production rate are shown together with measured energy consumption rate in terms of watt-hours per kilogram of distilled water produced.

Reveley, W. F.; Nuccio, P. P.

1975-01-01

179

RIS0-M-2319 RISK ANALYSIS OF A DISTILLATION UNIT  

E-print Network

.3.2. Boundaries for the analysis 11 1.3.3. Safety equipment fitted to the plant and . plant safety features 12 1.4. Improvements in procedures resulting from the study 89 9. Evaluation 89 A. Resources 89 B. Methods and criteria, the risk analysis methods used, experience of application of the methods, and a provisonal evaluation

180

New Design Methods And Algorithms For High Energy-Efficient And Low-cost Distillation Processes  

SciTech Connect

This project sought and successfully answered two big challenges facing the creation of low-energy, cost-effective, zeotropic multi-component distillation processes: first, identification of an efficient search space that includes all the useful distillation configurations and no undesired configurations; second, development of an algorithm to search the space efficiently and generate an array of low-energy options for industrial multi-component mixtures. Such mixtures are found in large-scale chemical and petroleum plants. Commercialization of our results was addressed by building a user interface allowing practical application of our methods for industrial problems by anyone with basic knowledge of distillation for a given problem. We also provided our algorithm to a major U.S. Chemical Company for use by the practitioners. The successful execution of this program has provided methods and algorithms at the disposal of process engineers to readily generate low-energy solutions for a large class of multicomponent distillation problems in a typical chemical and petrochemical plant. In a petrochemical complex, the distillation trains within crude oil processing, hydrotreating units containing alkylation, isomerization, reformer, LPG (liquefied petroleum gas) and NGL (natural gas liquids) processing units can benefit from our results. Effluents from naphtha crackers and ethane-propane crackers typically contain mixtures of methane, ethylene, ethane, propylene, propane, butane and heavier hydrocarbons. We have shown that our systematic search method with a more complete search space, along with the optimization algorithm, has a potential to yield low-energy distillation configurations for all such applications with energy savings up to 50%.

Agrawal, Rakesh

2013-11-21

181

Radiation hard vacuum switch  

DOEpatents

A vacuum switch with an isolated trigger probe which is not directly connected to the switching electrodes. The vacuum switch within the plasmatron is triggered by plasma expansion initiated by the trigger probe which travels through an opening to reach the vacuum switch elements. The plasma arc created is directed by the opening to the space between the anode and cathode of the vacuum switch to cause conduction.

Boettcher, Gordon E. (Albuquerque, NM)

1990-01-01

182

The Classical Vacuum.  

ERIC Educational Resources Information Center

The classical vacuum of physics is not empty, but contains a distinctive pattern of electromagnetic fields. Discovery of the vacuum, thermal spectrum, classical electron theory, zero-point spectrum, and effects of acceleration are discussed. Connection between thermal radiation and the classical vacuum reveals unexpected unity in the laws of…

Boyer, Timothy H.

1985-01-01

183

Preprototype vapor compression distillation subsystem. [recovering potable water from wastewater  

NASA Technical Reports Server (NTRS)

A three-person capacity preprototype vapor compression distillation subsystem for recovering potable water from wastewater aboard spacecraft was designed, assembled, and tested. The major components of the subsystem are: (1) a distillation unit which includes a compressor, centrifuge, central shaft, and outer shell; (2) a purge pump; (3) a liquids pump; (4) a post-treat cartridge; (5) a recycle/filter tank; (6) an evaporator high liquid level sensor; and (7) the product water conductivity monitor. A computer based control monitor instrumentation carries out operating mode change sequences, monitors and displays subsystem parameters, maintains intramode controls, and stores and displays fault detection information. The mechanical hardware occupies 0.467 m3, requires 171 W of electrical power, and has a dry weight of 143 kg. The subsystem recovers potable water at a rate of 1.59 kg/hr, which is equivalent to a duty cycle of approximately 30% for a crew of three. The product water has no foul taste or odor. Continued development of the subsystem is recommended for reclaiming water for human consumption as well as for flash evaporator heat rejection, urinal flushing, washing, and other on-board water requirements.

Ellis, G. S.; Wynveen, R. A.; Schubert, F. H.

1979-01-01

184

27 CFR 17.151 - Use of distilled spirits.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Use of distilled spirits. 17.151 Section 17.151 Alcohol...LIQUORS DRAWBACK ON TAXPAID DISTILLED SPIRITS USED IN MANUFACTURING NONBEVERAGE PRODUCTS Claims for Drawback Spirits Subject to Drawback § 17.151...

2010-04-01

185

40 CFR 721.9635 - Terpene residue distillates.  

...forth as follows: § 721.9635 Terpenes and terpenoids, limonene fraction, distn. residues, distillates. (a) Chemical...The chemical substance identified as terpenes and terpenoids, limonene fraction, distn. residues, distillates (PMN...

2014-07-01

186

40 CFR 1065.703 - Distillate diesel fuel.  

Code of Federal Regulations, 2013 CFR

...ENGINE-TESTING PROCEDURES Engine Fluids, Test Fuels...703 Distillate diesel fuel. (a) Distillate diesel fuels for testing...adequate for proper engine operation. (b...three grades of #2 diesel fuel...

2013-07-01

187

40 CFR 1065.703 - Distillate diesel fuel.  

Code of Federal Regulations, 2012 CFR

...ENGINE-TESTING PROCEDURES Engine Fluids, Test Fuels...703 Distillate diesel fuel. (a) Distillate diesel fuels for testing...adequate for proper engine operation. (b...three grades of #2 diesel fuel...

2012-07-01

188

40 CFR 1065.703 - Distillate diesel fuel.  

Code of Federal Regulations, 2010 CFR

...ENGINE-TESTING PROCEDURES Engine Fluids, Test Fuels...703 Distillate diesel fuel. (a) Distillate diesel fuels for testing...adequate for proper engine operation. (b...three grades of #2 diesel fuel...

2010-07-01

189

40 CFR 1065.703 - Distillate diesel fuel.  

Code of Federal Regulations, 2011 CFR

...ENGINE-TESTING PROCEDURES Engine Fluids, Test Fuels...703 Distillate diesel fuel. (a) Distillate diesel fuels for testing...adequate for proper engine operation. (b...three grades of #2 diesel fuel...

2011-07-01

190

40 CFR 1065.703 - Distillate diesel fuel.  

...ENGINE-TESTING PROCEDURES Engine Fluids, Test Fuels...703 Distillate diesel fuel. (a) Distillate diesel fuels for testing...adequate for proper engine operation. (b...three grades of #2 diesel fuel...

2014-07-01

191

Intelligent fuzzy supervisory control for distillation columns  

E-print Network

to be controlled. In many difficult process situations such as steelmaking furnaces [7], cement kilns [13], presses in the glass industry [4] and distillation columns [12], such models do not exist. While there are a variety of adaptive techniques which can...

Santhanam, Srinivasan

2012-06-07

192

Chemical composition of distillers grains, a review  

Technology Transfer Automated Retrieval System (TEKTRAN)

In recent years, increasing demand for ethanol as a fuel additive and decreasing dependency on fossil fuels have resulted in a dramatic increase in the amount of grains used for ethanol production. Dry-grind is the major process, resulting in distillers dried grains with solubles (DDGS) as a major ...

193

PPMCSA Presentation on Winter Distillate Outlook  

NSDL National Science Digital Library

This presentation on the Winter Distillate Outlook was created for the PPMCSA Meeting and Trade Show of this year. It gives basic information and forecasts on the prices of a variety of energy sources through a collection of slides and accompanying notes.

194

Distillation Calculations with a Programmable Calculator.  

ERIC Educational Resources Information Center

Describes a three-step approach for teaching multicomponent distillation to undergraduates, emphasizing patterns of distribution as an aid to understanding the separation processes. Indicates that the second step can be carried out by programmable calculators. (A more complete set of programs for additional calculations is available from the…

Walker, Charles A.; Halpern, Bret L.

1983-01-01

195

TOTAL REFLUX OPERATION OF MULTIVESSEL BATCH DISTILLATION  

E-print Network

the operation is switched between total re ux operation and dumping the product i.e., the condenser holdup products are collected in the condenser drum and in the reboiler. Another alternative is to "invert multivessel batch distillation column by calculating in advance the nal holdup in each vessel and then using

Skogestad, Sigurd

196

Acetylation of corn distillers dried grains  

Microsoft Academic Search

This paper shows that acidic conditions provide substantially higher % acetyl content, intrinsic viscosity and thermoplasticity even at low ratios of acetic anhydride and catalyst concentrations compared to using alkaline conditions for acetylation of oil-and-zein-free distillers dried grains with solubles (DDGS). Conventional methods of carbohydrate and protein acetylation are unsuitable for acetylating DDGS which is a mixture of carbohydrates and

Narendra Reddy; Chunyan Hu; Kelu Yan; Yiqi Yang

2011-01-01

197

Predicting Stability of Distiller’s Wet Grains (DWG) with Color Analysis  

Microsoft Academic Search

Distiller’s wet grain (DWG) is one of the coproducts from the fuel ethanol industry. Although many studies have investigated\\u000a the nutritional properties of DWG, little work has investigated the storability and shelf life for these feed products or\\u000a how to measure these quantities. The objectives of this research were to measure the development of microorganisms and their\\u000a respiration over time

K. A. Rosentrater; R. M. Lehman

2010-01-01

198

27 CFR 19.739 - Authorized transfers to or from distilled spirits plants.  

Code of Federal Regulations, 2012 CFR

...transfers to or from distilled spirits plants. 19.739 Section 19.739 Alcohol...TREASURY LIQUORS DISTILLED SPIRITS PLANTS Distilled Spirits for Fuel Use Transfer of Spirits to and from Distilled Spirits Plants § 19.739 Authorized transfers...

2012-04-01

199

27 CFR 19.739 - Authorized transfers to or from distilled spirits plants.  

...transfers to or from distilled spirits plants. 19.739 Section 19.739 Alcohol...TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Distilled Spirits for Fuel Use Transfer of Spirits to and from Distilled Spirits Plants § 19.739 Authorized transfers...

2014-04-01

200

27 CFR 19.739 - Authorized transfers to or from distilled spirits plants.  

Code of Federal Regulations, 2013 CFR

...transfers to or from distilled spirits plants. 19.739 Section 19.739 Alcohol...TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Distilled Spirits for Fuel Use Transfer of Spirits to and from Distilled Spirits Plants § 19.739 Authorized transfers...

2013-04-01

201

27 CFR 19.739 - Authorized transfers to or from distilled spirits plants.  

Code of Federal Regulations, 2011 CFR

...transfers to or from distilled spirits plants. 19.739 Section 19.739 Alcohol...TREASURY LIQUORS DISTILLED SPIRITS PLANTS Distilled Spirits for Fuel Use Transfer of Spirits to and from Distilled Spirits Plants § 19.739 Authorized transfers...

2011-04-01

202

Rejection and fate of trace organic compounds (TrOCs) during membrane distillation  

E-print Network

. Introduction Membrane distillation (MD) is a low temperature distillation process that involves the transportRejection and fate of trace organic compounds (TrOCs) during membrane distillation Kaushalya COCs) Direct contact membrane distillation (DCMD) Volatility Fate and transport Hydrophobicity

203

27 CFR 19.162 - Operations bond for distilled spirits plant and adjacent bonded wine cellar.  

Code of Federal Regulations, 2013 CFR

...for a distilled spirits plant and adjacent bonded wine...Such distilled spirits plant is qualified under subpart D of this part for the production of distilled spirits; and...cellar and distilled spirits plant are operated by the...

2013-04-01

204

27 CFR 19.241 - Operations bond-distilled spirits plant and adjacent bonded wine cellar.  

Code of Federal Regulations, 2010 CFR

...being adjacent to a distilled spirits plant if— (1) Such distilled spirits plant is qualified under subpart G for the production of distilled spirits; and ...wine cellar and distilled spirits plant are operated by the same...

2010-04-01

205

27 CFR 19.162 - Operations bond for distilled spirits plant and adjacent bonded wine cellar.  

...for a distilled spirits plant and adjacent bonded wine...Such distilled spirits plant is qualified under subpart D of this part for the production of distilled spirits; and...cellar and distilled spirits plant are operated by the...

2014-04-01

206

27 CFR 19.162 - Operations bond for distilled spirits plant and adjacent bonded wine cellar.  

Code of Federal Regulations, 2011 CFR

...for a distilled spirits plant and adjacent bonded wine...Such distilled spirits plant is qualified under subpart D of this part for the production of distilled spirits; and...cellar and distilled spirits plant are operated by the...

2011-04-01

207

27 CFR 19.162 - Operations bond for distilled spirits plant and adjacent bonded wine cellar.  

Code of Federal Regulations, 2012 CFR

...for a distilled spirits plant and adjacent bonded wine...Such distilled spirits plant is qualified under subpart D of this part for the production of distilled spirits; and...cellar and distilled spirits plant are operated by the...

2012-04-01

208

27 CFR 1.82 - Acquiring or receiving distilled spirits in bulk for redistillation, processing, rectification...  

Code of Federal Regulations, 2010 CFR

...false Acquiring or receiving distilled spirits in bulk for redistillation, processing...ADMINISTRATION ACT, NONINDUSTRIAL USE OF DISTILLED SPIRITS AND WINE, BULK SALES AND BOTTLING OF DISTILLED SPIRITS Bulk Sales and Bottling of Distilled...

2010-04-01

209

27 CFR 1.84 - Acquisition of distilled spirits in bulk by Government agencies.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Acquisition of distilled spirits in bulk by Government agencies. 1.84...ADMINISTRATION ACT, NONINDUSTRIAL USE OF DISTILLED SPIRITS AND WINE, BULK SALES AND BOTTLING OF DISTILLED SPIRITS Bulk Sales and Bottling of Distilled...

2010-04-01

210

27 CFR 17.163 - Evidence of taxpayment of distilled spirits.  

Code of Federal Regulations, 2010 CFR

... Evidence of taxpayment of distilled spirits. 17.163 Section 17.163 Alcohol...LIQUORS DRAWBACK ON TAXPAID DISTILLED SPIRITS USED IN MANUFACTURING NONBEVERAGE PRODUCTS... Evidence of taxpayment of distilled spirits. (a) Shipments from distilled...

2010-04-01

211

27 CFR 1.83 - Acquiring or receiving distilled spirits in bulk for addition to wine.  

Code of Federal Regulations, 2010 CFR

...false Acquiring or receiving distilled spirits in bulk for addition to wine. 1.83...ADMINISTRATION ACT, NONINDUSTRIAL USE OF DISTILLED SPIRITS AND WINE, BULK SALES AND BOTTLING OF DISTILLED SPIRITS Bulk Sales and Bottling of Distilled...

2010-04-01

212

DIRECT COMPUTATIONS TO DESCRIBE BATCH DISTILLATION WITH RECTIFICATION  

Microsoft Academic Search

An analog of the Rayleigh Equation has been applied for many years to describe batch distillation with rectification for binary mixtures. A solution is obtained by iterative graphical computations followed by numerical integration. When the batch distillation algorithm is stated in terms of distillate composition a computational non-iterative soluton may be obtained. For a binary separation this expression may be

RAYMOND C. WAGGONER

1990-01-01

213

Continuous and Batch Distillation in an Oldershaw Tray Column  

ERIC Educational Resources Information Center

The importance of distillation in the separation field prompts the inclusion of distillation experiments in the chemical engineering curricula. This work describes the performance of an Oldershaw column in the rectification of a cyclohexane/n-heptane mixture. Total reflux distillation, continuous rectification under partial reflux, and batch…

Silva, Carlos M.; Vaz, Raquel V.; Santiago, Ana S.; Lito, Patricia F.

2011-01-01

214

Key Distillation and the Secret-Bit Fraction  

Microsoft Academic Search

We consider distillation of secret bits from partially secret noisy correlations , shared between two honest par- ties and an eavesdropper. The most studied distillation scenario consists of joint operations on a large number of copies of the distribution , assisted with public communication. Here we consider distillation with only one copy of the distribution, and instead of rates, the

Nick S. Jones; Lluis Masanes

2006-01-01

215

Distillation and solvent extraction process for rerefining used lubricating oil  

Microsoft Academic Search

Used oil is rerefined by distillation and extraction with tetrahydrofurfuryl alcohol. In accordance with the process, used oil is rerefined by distillation to remove a volatile forecut followed by further distillation with recirculation provisions to obtain the desired fractions of lubricating oil products while reducing the vaporization temperature of the oil. The recycle effect tends to reduce coking and cracking

H. J. Beard; L. C. Fletcher; R. Oblasny

1982-01-01

216

Wireless Integrated Microelectronic Vacuum Sensor System  

NASA Technical Reports Server (NTRS)

NASA Stennis Space Center's (SSC's) large rocket engine test facility requires the use of liquid propellants, including the use of cryogenic fluids like liquid hydrogen as fuel, and liquid oxygen as an oxidizer (gases which have been liquefied at very low temperatures). These fluids require special handling, storage, and transfer technology. The biggest problem associated with transferring cryogenic liquids is product loss due to heat transfer. Vacuum jacketed piping is specifically designed to maintain high thermal efficiency so that cryogenic liquids can be transferred with minimal heat transfer. A vacuum jacketed pipe is essentially two pipes in one. There is an inner carrier pipe, in which the cryogenic liquid is actually transferred, and an outer jacket pipe that supports and seals the vacuum insulation, forming the "vacuum jacket." The integrity of the vacuum jacketed transmission lines that transfer the cryogenic fluid from delivery barges to the test stand must be maintained prior to and during engine testing. To monitor the vacuum in these vacuum jacketed transmission lines, vacuum gauge readings are used. At SSC, vacuum gauge measurements are done on a manual rotation basis with two technicians, each using a handheld instrument. Manual collection of vacuum data is labor intensive and uses valuable personnel time. Additionally, there are times when personnel cannot collect the data in a timely fashion (i.e., when a leak is detected, measurements must be taken more often). Additionally, distribution of this data to all interested parties can be cumbersome. To simplify the vacuum-gauge data collection process, automate the data collection, and decrease the labor costs associated with acquiring these measurements, an automated system that monitors the existing gauges was developed by Invocon, Inc. For this project, Invocon developed a Wireless Integrated Microelectronic Vacuum Sensor System (WIMVSS) that provides the ability to gather vacuum-gauge measurements automatically and wirelessly, in near-real time - using a low-maintenance, lowpower sensor mesh network. The WIMVSS operates by using a self-configuring mesh network of wireless sensor units. Mesh networking is a type of networking where each sensor or node can capture and disseminate its own data, but also serve as a relay to receive and transmit data from other sensors. Each sensor node can synchronize with adjacent sensors, and propagate data from one sensor to the next, until the destination is reached. In this case, the destination is a Network Interface Unit (NIU). The WIMVSS sensors are mounted on the existing vacuum gauges. Information gathered by the sensors is sent to the NIU. Because of the mesh networking, if a sensor cannot directly send the data to the NIU, it can be propagated through the network of sensors. The NIU requires antenna access to the sensor units, AC power, and an Ethernet connection. The NIU bridges the sensor network to a WIMVSS server via an Ethernet connection. The server is configured with a database, a Web server, and proprietary interface software that makes it possible for the vacuum measurements from vacuum jacketed fluid lines to be saved, retrieved, and then displayed from any Web-enabled PC that has access to the Internet. Authorized users can then simply access the data from any PC with Internet connection. Commands can also be sent directly from the Web interface for control and maintenance of the sensor network. The technology enabled by the WIMVSS decreases labor required for gathering vacuum measurements, increases access to vacuum data by making it available on any computer with access to the Internet, increases the frequency with which data points can be acquired for evaluating the system, and decreases the recurring cost of the sensors by using off-the-shelf components and integrating these with heritage vacuum gauges.

Krug, Eric; Philpot, Brian; Trott, Aaron; Lawrence, Shaun

2013-01-01

217

Secret key distillation from shielded two-qubit states  

SciTech Connect

The quantum states corresponding to a secret key are characterized using the so-called private states, where the key part consisting of a secret key is shielded by the additional systems. Based on the construction, it was shown that a secret key can be distilled from bound entangled states. In this work, I consider the shielded two-qubit states in a key-distillation scenario and derive the conditions under which a secret key can be distilled using the recurrence protocol or the two-way classical distillation, advantage distillation together with one-way postprocessing. From the security conditions, it is shown that a secret key can be distilled from bound entangled states in a much wider range. In addition, I consider the case that in which white noise is added to quantum states and show that the classical distillation protocol still works despite a certain amount of noise although the recurrence protocol does not.

Bae, Joonwoo [School of Computational Sciences, Korea Institute for Advanced Study, Seoul 130-722 (Korea, Republic of)

2010-05-15

218

Secret key distillation from shielded two-qubit states  

E-print Network

The quantum states corresponding to a secret key are characterized using the so-called private states, where the key part consisting of a secret key is shielded by the additional systems. Based on the construction, it was shown that a secret key can be distilled from bound entangled states. In this work, I consider the shielded two-qubit states in a key-distillation scenario and derive the conditions under which a secret key can be distilled using the recurrence protocol or the two-way classical distillation, advantage distillation together with one-way postprocessing. From the security conditions, it is shown that a secret key can be distilled from bound entangled states in a much wider range. In addition, I consider the case that in which white noise is added to quantum states and show that the classical distillation protocol still works despite a certain amount of noise although the recurrence protocol does not.

Joonwoo Bae

2008-03-03

219

Contact structure for use in catalytic distillation  

DOEpatents

A method for conducting catalytic chemical reactions and fractionation of the reaction mixture comprising feeding reactants into a distillation column reactor contracting said reactant in liquid phase with a fixed bed catalyst in the form of a contact catalyst structure consisting of closed porous containers containing the catatlyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column.

Jones, Jr., Edward M. (Friendswood, TX)

1984-01-01

220

Contact structure for use in catalytic distillation  

DOEpatents

A method and apparatus for conducting catalytic chemical reactions and fractionation of the reaction mixture, comprising and feeding reactants into a distillation column reactor contracting said reactant in a liquid phase with a fixed bed catalyst in the form of a contact catalyst structure, consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column.

Jones, Jr., Edward M. (Friendswood, TX)

1985-01-01

221

Contact structure for use in catalytic distillation  

DOEpatents

A method and apparatus are disclosed for conducting catalytic chemical reactions and fractionation of the reaction mixture, comprising and feeding reactants into a distillation column reactor contracting said reactant in a liquid phase with a fixed bed catalyst in the form of a contact catalyst structure, consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column. 7 figs.

Jones, E.M. Jr.

1985-08-20

222

Contact structure for use in catalytic distillation  

DOEpatents

A method is described for conducting catalytic chemical reactions and fractionation of the reaction mixture comprising feeding reactants into a distillation column reactor, contracting said reactant in liquid phase with a fixed bed catalyst in the form of a contact catalyst structure consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column. 7 figs.

Jones, E.M. Jr.

1984-03-27

223

Solar desalination by freezing and distillation  

NASA Astrophysics Data System (ADS)

It is noted that among seawater desalination processes the absorption-freeze vapor compression processes based on the thermal heat pump, although untested commercially and still in the development stage, appears technically and economically an attractive application of low-grade (exergy) solar heat. The distillation processes proposed here may be conveniently powered by low-grade solar heat (from flat plate solar collectors). It is expected that the scaling problem will be insignificant in comparison with that encountered in the conventional multistage flash process. The novel feature here is the use of enlarged capacity for heat exchange between distillate and brine via latent heat of solid-liquid phase change of a suitable hydrophobic intermediate heat transfer material.

Kvajic, G.

224

Attractor mechanism as a distillation procedure  

SciTech Connect

In a recent paper it was shown that for double extremal static spherical symmetric BPS black hole solutions in the STU model the well-known process of moduli stabilization at the horizon can be recast in a form of a distillation procedure of a three-qubit entangled state of a Greenberger-Horne-Zeilinger type. By studying the full flow in moduli space in this paper we investigate this distillation procedure in more detail. We introduce a three-qubit state with amplitudes depending on the conserved charges, the warp factor, and the moduli. We show that for the recently discovered non-BPS solutions it is possible to see how the distillation procedure unfolds itself as we approach the horizon. For the non-BPS seed solutions at the asymptotically Minkowski region we are starting with a three-qubit state having seven nonequal nonvanishing amplitudes and finally at the horizon we get a Greenberger-Horne-Zeilinger state with merely four nonvanishing ones with equal magnitudes. The magnitude of the surviving nonvanishing amplitudes is proportional to the macroscopic black hole entropy. A systematic study of such attractor states shows that their properties reflect the structure of the fake superpotential. We also demonstrate that when starting with the very special values for the moduli corresponding to flat directions the uniform structure at the horizon deteriorates due to errors generalizing the usual bit flips acting on the qubits of the attractor states.

Levay, Peter; Szalay, Szilard [Department of Theoretical Physics, Institute of Physics, Budapest University of Technology and Economics, H-1521 Budapest (Hungary)

2010-07-15

225

The distillation and volatility of ionic liquids  

NASA Astrophysics Data System (ADS)

It is widely believed that a defining characteristic of ionic liquids (or low-temperature molten salts) is that they exert no measurable vapour pressure, and hence cannot be distilled. Here we demonstrate that this is unfounded, and that many ionic liquids can be distilled at low pressure without decomposition. Ionic liquids represent matter solely composed of ions, and so are perceived as non-volatile substances. During the last decade, interest in the field of ionic liquids has burgeoned, producing a wealth of intellectual and technological challenges and opportunities for the production of new chemical and extractive processes, fuel cells and batteries, and new composite materials. Much of this potential is underpinned by their presumed involatility. This characteristic, however, can severely restrict the attainability of high purity levels for ionic liquids (when they contain poorly volatile components) in recycling schemes, as well as excluding their use in gas-phase processes. We anticipate that our demonstration that some selected families of commonly used aprotic ionic liquids can be distilled at 200-300°C and low pressure, with concomitant recovery of significant amounts of pure substance, will permit these currently excluded applications to be realized.

Earle, Martyn J.; Esperança, José M. S. S.; Gilea, Manuela A.; Canongia Lopes, José N.; Rebelo, Luís P. N.; Magee, Joseph W.; Seddon, Kenneth R.; Widegren, Jason A.

2006-02-01

226

Distillation Designs for the Lunar Surface  

NASA Technical Reports Server (NTRS)

Gravity-based distillation methods may be applied to the purification of wastewater on the lunar base. These solutions to water processing are robust physical separation techniques, which may be more advantageous than many other techniques for their simplicity in design and operation. The two techniques can be used in conjunction with each other to obtain high purity water. The components and feed compositions for modeling waste water streams are presented in conjunction with the Aspen property system for traditional stage distillation. While the individual components for each of the waste streams will vary naturally within certain bounds, an analog model for waste water processing is suggested based on typical concentration ranges for these components. Target purity levels for recycled water are determined for each individual component based on NASA s required maximum contaminant levels for potable water Optimum parameters such as reflux ratio, feed stage location, and processing rates are determined with respect to the power consumption of the process. Multistage distillation is evaluated for components in wastewater to determine the minimum number of stages necessary for each of 65 components in humidity condensate and urine wastewater mixed streams.

Boul, Peter J.; Lange,Kevin E.; Conger, Bruce; Anderson, Molly

2010-01-01

227

Vacuum probe surface sampler  

NASA Technical Reports Server (NTRS)

A vacuum probe surface sampler is described for rapidly sampling relatively large surface areas which possess relatively light loading densities of micro-organism, drug particles or the like. A vacuum head with a hollow handle connected to a suitable vacuum source is frictionally attached to a cone assembly terminating in a flared tip adapted to be passed over the surface to be sampled. A fine mesh screen carried by the vacuum head provides support for a membrane filter which collects the microorganisms or other particles. The head assembly is easily removed from the cone assembly without contacting the cone assembly with human hands.

Zahlava, B. A. (inventor)

1973-01-01

228

NSLS II Vacuum System  

SciTech Connect

National Synchrotron Light Source II, being constructed at Brookhaven, is a 3-GeV, 500 mA, 3rd generation synchrotron radiation facility with ultra low emittance electron beams. The storage ring vacuum system has a circumference of 792 m and consists of over 250 vacuum chambers with a simulated average operating pressure of less than 1 x 10{sup -9} mbar. A summary of the update design of the vacuum system including girder supports of the chambers, gauges, vacuum pumps, bellows, beam position monitors and simulation of the average pressure will be shown. A brief description of the techniques and procedures for cleaning and mounting the chambers are given.

Ferreira, M.; Doom, L.; Hseuh, H.; Longo, C.; Settepani, P.; Wilson, K.; Hu, J.

2009-09-13

229

Heavy wax distillate as a raw material for the production of solid hydrocarbons  

SciTech Connect

This article discusses the feasibility of recovering solid hydrocarbons from a heavy wax distillate in order to expand the raw material base for the production of high-melting waxes. The examined distillate has a melting point of 45/sup 0/C, a wax content of 34% by weight, a viscosity (at 100/sup 0/C) of 8.2 mm/sup 2//sec, a molecular weight of 345, a content of paraffinic and naphthenic hydrocarbons of 59.1% by weight, contents of aromatic hydrocarbons (light, medium and heavy) of 8.9%, 5.1%, and 20.4% by weight, respectively, and a content of hydrocarbons forming and not forming urea adducts of 21.8% and 78.2%, respectively. The heavy wax distillate was filtered in a Bogdanov laboratory unit containing a filter press consisting of a crystallizer and a slack wax chamber. The filtration residue from the crystallizer beaker and the slack wax cake from the wax chamber are collected in a preweighed container. It is concluded that the heavy wax distillate can be successfully dewaxed for wax production if it is modified by dilution with a filtrate and the incorporation of a structure modifier.

Gundyrev, R.A.; Fokina, T.V.; Garun, Y.E.; Kazakova, L.P.; Sochevko, T.I.

1984-07-01

230

Apparatus for distilling shale oil from oil shale  

SciTech Connect

An apparatus for distilling shale oil from oil shale comprises: a vertical type distilling furnace which is divided by two vertical partitions each provided with a plurality of vent apertures into an oil shale treating chamber and two gas chambers, said oil shale treating chamber being located between said two gas chambers in said vertical type distilling furnace, said vertical type distilling furnace being further divided by at least one horizontal partition into an oil shale distilling chamber in the lower part thereof and at least one oil shale preheating chamber in the upper part thereof, said oil shale distilling chamber and said oil shale preheating chamber communication with each other through a gap provided at an end of said horizontal partition, an oil shale supplied continuously from an oil shale supply port provided in said oil shale treating chamber at the top thereof into said oil shale treating chamber continuously moving from the oil shale preheating chamber to the oil shale distilling chamber, a high-temperature gas blown into an oil shale distilling chamber passing horizontally through said oil shale in said oil shale treating chamber, thereby said oil shale is preheated in said oil shale preheating chamber, and a gaseous shale oil is distilled from said preheated oil shale in said oil shale distilling chamber; and a separator for separating by liquefaction a gaseous shale oil from a gas containing the gaseous shale oil discharged from the oil shale preheating chamber.

Shishido, T.; Sato, Y.

1984-02-14

231

Fractionation of distillers dried grains with solubles (DDGS) through a narrowing of particle size distribution followed by aspiration  

Technology Transfer Automated Retrieval System (TEKTRAN)

Distillers dried grains with solubles (DDGS) may have more value and utility if they can be separated into high protein and high fiber fractions. A variety of such separation processes have been proposed; two of the most promising processes involve 3 screening and 3 air classification unit operatio...

232

Characterization of Chemical and Physical Properties of Distillers Dried Grains with Solubles (DDSG) for Value Added Uses  

Technology Transfer Automated Retrieval System (TEKTRAN)

One of the fastest growing industries in the United States is the fuel ethanol industry. Since 2000 there has been an increase of more than 300%. There was production of 4.9 billion gallons of ethanol in the year 2006. The major coproducts from this industry include Distillers Dried Grains with Solu...

233

Vacuum Vessel Remote Handling  

E-print Network

FIRE Vacuum Vessel and Remote Handling Overview B. Nelson, T. Burgess, T. Brown, H-M Fan, G. Jones · Vacuum Vessel - Design requirements - Design concept and features - Analysis to date - Status and summary Replacement Time Estimates - Balance of RH Equipment · Design and analysis are consistent with pre

234

The ultimate vacuum  

Microsoft Academic Search

The ultimate vacuum, defined as the lowest pressure that can be produced and measured reproducibly in a vacuum system at room temperature, has decreased by a factor of about 1014 since the first measurement of sub-atmospheric pressure by Robert Boyle in about 1660. A brief historical review is presented of the key advances that caused significant decreases in the ultimate

P. A. Redhead

1999-01-01

235

Microfabricated triggered vacuum switch  

DOEpatents

A microfabricated vacuum switch is disclosed which includes a substrate upon which an anode, cathode and trigger electrode are located. A cover is sealed over the substrate under vacuum to complete the vacuum switch. In some embodiments of the present invention, a metal cover can be used in place of the trigger electrode on the substrate. Materials used for the vacuum switch are compatible with high vacuum, relatively high temperature processing. These materials include molybdenum, niobium, copper, tungsten, aluminum and alloys thereof for the anode and cathode. Carbon in the form of graphitic carbon, a diamond-like material, or carbon nanotubes can be used in the trigger electrode. Channels can be optionally formed in the substrate to mitigate against surface breakdown.

Roesler, Alexander W. (Tijeras, NM); Schare, Joshua M. (Albuquerque, NM); Bunch, Kyle (Albuquerque, NM)

2010-05-11

236

ELETTRA vacuum system  

NASA Astrophysics Data System (ADS)

A status report of the vacuum system of ELETTRA, the 2 GeV, 400 mA light source under construction in Trieste, will be described. The Vacuum project, presented at ``Synchrotron Radiation Vacuum Workshop'' at Riken (Japan 22-24 March 1990) and more recently at EVC-2, the European Vacuum Conference at Trieste (Italy 21-26 May 1990), is now in the phase of testing a prototype sector, which is 1/24 of the ring circumference. Details and some technological aspects of the fabrication will be reviewed together with the vacuum performances. Results of laboratory experiments on components, standard or not, allowed us to finalize the main choices in light of the general philosophy of the project and will be properly summarized.

Bernardini, M.

1991-08-01

237

Surface code implementation of block code state distillation  

PubMed Central

State distillation is the process of taking a number of imperfect copies of a particular quantum state and producing fewer better copies. Until recently, the lowest overhead method of distilling states produced a single improved |A? state given 15 input copies. New block code state distillation methods can produce k improved |A? states given 3k + 8 input copies, potentially significantly reducing the overhead associated with state distillation. We construct an explicit surface code implementation of block code state distillation and quantitatively compare the overhead of this approach to the old. We find that, using the best available techniques, for parameters of practical interest, block code state distillation does not always lead to lower overhead, and, when it does, the overhead reduction is typically less than a factor of three. PMID:23736868

Fowler, Austin G.; Devitt, Simon J.; Jones, Cody

2013-01-01

238

Final Report, Distillation Column Flooding Predictor  

SciTech Connect

The Flooding Predictor is an advanced process control strategy comprising a patented pattern-recognition methodology that identifies pre-flood patterns discovered to precede flooding events in distillation columns. The grantee holds a U.S. patent on the modeling system. The technology was validated at the Separations Research Program, The University of Texas at Austin under a grant from the U. S. Department of Energy, Inventions & Innovation Program. Distillation tower flooding occurs at abnormally high vapor and/or liquid rates. The loss in tray efficiencies is attributed to unusual behavior of liquid inventories inside the column leading to conditions of flooding of the space in between trays with liquid. Depending on the severity of the flood condition, consequences range from off spec products to equipment damage and tower shutdown. This non-intrusive pattern recognition methodology, processes signal data obtained from existing column instrumentation. Once the pattern is identified empirically, it is modeled and coded into the plant's distributed control system. The control system is programmed to briefly "unload" the tower each time the pattern appears. The unloading takes the form of a momentary reduction in column severity, e.g., decrease bottom temperature, reflux or tower throughput. Unloading the tower briefly at the pre-flood state causes long-term column operation to become significantly more stable - allowing an increase in throughput and/or product purity. The technology provides a wide range of value between optimization and flooding. When a distillation column is not running at capacity, it should be run in such a way ("pushed") that optimal product purity is achieved. Additional benefits include low implementation and maintenance costs, and a high level of console operator acceptance. The previous commercial applications experienced 98% uptime over a four-year period. Further, the technology is unique in its ability to distinguish between different flooding mechanisms within the same tower, e.g., liquid and jet flooding.

George E. Dzyacky

2003-05-31

239

ZIRCONIUM CORROSION IN DISTILLED WATER AT 85  

Microsoft Academic Search

Zr corrosion in distilled water (pH = 6.5, SOâ = 0.6 mg\\/l) at 85 ; deg C in contact with 1 x 18H9T steel (0.l2% C, 0.50% Si, l.30% Mn, 18.13% Cr, ; 9.8% Ni, and 0.55% Ti) and with aluminum AlM (0.22 Fe, 0.06 Si, and <0.01 Cu) at ; a surface ratio of 1: 1 was investigated. The

V. V. Gerasimov; A. I. Gromova; E. T. Shapovalov

1961-01-01

240

Distillation and the Role of Weak Forces  

NSDL National Science Digital Library

In this activity, by the Concord Consortium's Molecular Literacy project, students will examine how distillation works and the roles of all components involved in the process. The site is filled with thorough diagrams accompanied by solid textual explanations. Aside from diagrams and text, students will engage in simple quizzes testing the concepts they have just learned. The activity itself is a java-based interactive resource built upon the free, open source Molecular Workbench software. In addition, visitors will find an overview of the activity, assessments, and concepts and their correlation to AAAS and NSES standards.

2008-10-17

241

Drum drying performance of condensed distillers solubles and comparison to performance of modified condensed distillers solubles  

Technology Transfer Automated Retrieval System (TEKTRAN)

Condensed distillers solubles (CDS) is a viscous, syrupy co-product of ethanol production from corn; CDS exhibits strong recalcitrance to drying due to its chemical composition, which includes a substantial amount of glycerol. The objectives of this study were to determine the drum drying performan...

242

Vapor compression distiller and membrane technology for water revitalization  

NASA Technical Reports Server (NTRS)

Water revitalization for a space station can consist of membrane filtration processes and a distillation process. Water recycling equipment using membrane filtration processes was manufactured for ground testing. It was assembled using commercially available components. Two systems for the distillation are studied: one is absorption type thermopervaporation cell and the other is a vapor compression distiller. Absorption type thermopervaporation, able to easily produce condensed water under zero gravity, was investigated experimentally and through simulated calculation. The vapor compression distiller was studied experimentally and it offers significant energy savings for evaporation of water.

Ashida, A.; Mitani, K.; Ebara, K.; Kurokawa, H.; Sawada, I.; Kashiwagi, H.; Tsuji, T.; Hayashi, S.; Otsubo, K.; Nitta, K.

1987-01-01

243

Evading death by vacuum  

NASA Astrophysics Data System (ADS)

In the Standard Model, the Higgs potential allows only one minimum at tree level. But the open possibility that there might be two scalar doublets enriches the vacuum structure, allowing for the risk that we might now be in a metastable state, which we dub the panic vacuum. Current experiments at the LHC are probing the Higgs particle predicted as a result of the spontaneous symmetry breaking. Remarkably, in the two Higgs model with a softly broken U(1) symmetry, the LHC experiments already allow to exclude many panic vacuum solutions.

Barroso, A.; Ferreira, P. M.; Ivanov, I. P.; Santos, Rui; Silva, João P.

2013-09-01

244

Evading death by vacuum  

E-print Network

In the Standard Model, the Higgs potential allows only one minimum at tree-level. But the open possibility that there might be two scalar doublets enriches the vacuum structure, allowing for the risk that we might now be in a metastable state, which we dub the panic vacuum. Current experiments at the LHC are probing the Higgs particle predicted as a result of the spontaneous symmetry breaking. Remarkably, in the two Higgs model with a softly broken U(1) symmetry, the LHC experiments already preclude panic vacuum solutions.

A. Barroso; P. M. Ferreira; I. P. Ivanov; Rui Santos; João P. Silva

2012-11-26

245

ANALYSES OF FISH TISSUE BY VACUUM DISTILLATION/GAS CHROMATOGRAPHY/MASS SPECTROMETRY  

EPA Science Inventory

The analyses of fish tissue using VD/GC/MS with surrogate-based matrix corrections is described. Techniques for equilibrating surrogate and analyte spikes with a tissue matrix are presented, and equilibrated spiked samples are used to document method performance. The removal of a...

246

SCREENING PROCESSED MILK FOR VOLATILE ORGANIC COMPOUNDS USING VACUUM DISTILLATION/GAS CHROMATOGRAPHY/MASS SPECTROMETRY  

EPA Science Inventory

An adaptation of Office of Solid Waste and Emergency Response' Test Methods for Evaluating Solid Waste Physical/Chemical Methods (SW-846) method 8261 to analyze milk for an expanded list of volatile organic compounds is presented. The milk matriz exhibits a strong affinity for o...

247

Pumpdown and Vacuum Pumps  

NSDL National Science Digital Library

This is a link to a PDF version of lecture slides that discuss vacuum pumpdown. Graphics are included which depict pumpdown procedure, venting procedure, pressure curves and system pumpdown. Keywords: Outgassing, pressure range, rotary vane, rotary piston, roots blower

Rack, Philip D.

248

Estimating vent emissions from a distillation column: An alternative to stack testing  

SciTech Connect

This technical paper points out the cost-effectiveness and data manageability of material balance over the epidemic use of stack testing in the chemical industry. An example is drawn from a Title V emissions inventory prepared for an international manufacturer of pharmaceuticals and fuel additives. This example case focuses on the use of mass balance to estimate noncondensibles generated by a typical large-scale distillation column. Distillation fundamentals are reviewed, including discussion of relative volatility, x-y and McCabe-Thiele diagrams, and basic sieve tray mechanics. A seemingly complex set of energy and material balance equations is simplified by the application of constant molar overflow. The example case concludes with a calculation of column noncondensibles, and the paper closes with a review of the material balance approach, including its strengths, limitations, and applicability to other unit operations.

Dickerson, D.L. Jr. [ERM-Southeast, Charleston, SC (United States)

1996-12-31

249

Distillation and condensation of LiCl-KCl eutectic salts for a separation of pure salts from salt wastes from an electrorefining process  

NASA Astrophysics Data System (ADS)

Salt separation and recovery from the salt wastes generated from a pyrochemical process is necessary to minimize the high-level waste volumes and to stabilize a final waste form. In this study, the thermal behavior of the LiCl-KCl eutectic salts containing rare earth oxychlorides or oxides was investigated during a vacuum distillation and condensation process. LiCl was more easily vaporized than the other salts (KCl and LiCl-KCl eutectic salt). Vaporization characteristics of LiCl-KCl eutectic salts were similar to that of KCl. The temperature to obtain the vaporization flux (0.1 g min -1 cm -2) was decreased by much as 150 °C by a reduction of the ambient pressure from 5 Torr to 0.5 Torr. Condensation behavior of the salt vapors was different with the ambient pressure. Almost all of the salt vapors were condensed and were formed into salt lumps during a salt distillation at the ambient pressure of 0.5 Torr and they were collected in the condensed salt storage. However, fine salt particles were formed when the salt distillation was performed at 10 Torr and it is difficult for them to be recovered. Therefore, it is thought that a salt vacuum distillation and condensation should be performed to recover almost all of the vaporized salts at a pressure below 0.5 Torr.

Eun, Hee Chul; Yang, Hee Chul; Lee, Han Soo; Kim, In Tae

2009-12-01

250

Azeotropic Distillation as a Technique for Emulsion Size Reduction  

E-print Network

: A solvent with HA Boiling point with water Heptane or Hexane Low vapor pressure viscosifying oil Distillation setup/ process -Found the Heterogeneous Azeotropic Distillation Boiling points for Water on microscope - Took several images at different time points - Took pictures in color also to see what was water

Petta, Jason

251

CHEM333: Experiment 4: Steam Distillation of Essential Oils;  

E-print Network

of an aqueous mixture but at a much lower/ less destructive temperature than distilling the compound directly for a dropping funnel. The water initially in your round bottom flask will be sufficient for the distillation, but they are obviously required. Boil the mixture vigorously, but watch for boil-overs! Collect about 125 m

Taber, Douglass

252

Sorption Isotherm Characteristics of Dried Distillers Grains with Solubles (DDGS)  

Technology Transfer Automated Retrieval System (TEKTRAN)

Distillers Dried Grains with Solubles (DDGS) is widely recognized as a highly nutritious animal feed ingredient. With the exponential growth of the fuel ethanol industry in the past several years, significant quantities of distillers grains are now being produced. To effectively utilize these feeds ...

253

Dynamic catalytic distillation: Advanced simulation and experimental validation  

Microsoft Academic Search

Reactive distillation offers a number of potential advantages, so that many traditional operations are currently being investigated in order to discover further applications of this technology. Increasingly, it is performed in columns with catalytic packings that combine the advantages of normal structured packings and heterogeneous catalysts. Analysis of reactive distillation is difficult due to strong physico-chemical interactions, and it is

L. U. Kreul; A. Górak; C. Dittrich; P. I. Barton

1998-01-01

254

Estimation of convective mass transfer in solar distillation systems  

Microsoft Academic Search

In this article a thermal model has been developed to determine the convective mass transfer for different Grashof Number range in solar distillatiOn process. The model is based on simple regression analysis. Based on the experimental data obtained from the rigorous outdoor experimentation on passive and active distillation systems for summer climatic conditions, the values of C and n have

Sanjay Kumar; G. N. Tiwari

1996-01-01

255

Teaching and Learning Distillation in Chemistry Laboratory Courses.  

ERIC Educational Resources Information Center

Distillation in the chemistry laboratory is an essential part of a practicing chemists' and a chemistry educators' work. Nevertheless, regardless of the degree of importance in each of the aforementioned professions, few educational studies on teaching and learning distillation exist. In an effort to rectify this oversight, the Department of…

van Keulen, Hanno; And Others

256

Distillation with Vapour Compression. An Undergraduate Experimental Facility.  

ERIC Educational Resources Information Center

Discusses the need to design distillation columns that are more energy efficient. Describes a "design and build" project completed by two college students aimed at demonstrating the principles of vapour compression distillation in a more energy efficient way. General design specifications are given, along with suggestions for teaching and…

Pritchard, Colin

1986-01-01

257

Teaching and Learning Distillation in Chemistry Laboratory Courses.  

ERIC Educational Resources Information Center

Investigated the problems chemistry majors have with learning distillation concepts in traditional chemistry laboratory courses. Reports that students take the generalized concepts at face value, construct decontextualized concepts for distillation, and cannot interpret their observations or make reasoned decisions based on the theoretical…

Keulen, Hanno van; And Others

1995-01-01

258

Modeling the flow properties of distillers dried grains with solubles  

Technology Transfer Automated Retrieval System (TEKTRAN)

Distillers dried grains with solubles (DDGS) are an excellent source of energy, minerals, and bypass protein for ruminants, and are also used in monogastric rations as well. With the remarkable growth of the US fuel ethanol industry in the past decade, large quantities of distillers grains are now b...

259

27 CFR 24.183 - Use of distillates containing aldehydes.  

Code of Federal Regulations, 2012 CFR

...containing aldehydes may be received on wine premises for use in the fermentation of wine and then returned to the distilled spirits plant...Distillates produced from one kind of fruit may not be used in the fermentation of wine made from a different kind of fruit....

2012-04-01

260

27 CFR 24.183 - Use of distillates containing aldehydes.  

Code of Federal Regulations, 2010 CFR

...containing aldehydes may be received on wine premises for use in the fermentation of wine and then returned to the distilled spirits plant...Distillates produced from one kind of fruit may not be used in the fermentation of wine made from a different kind of fruit....

2010-04-01

261

27 CFR 24.183 - Use of distillates containing aldehydes.  

Code of Federal Regulations, 2013 CFR

...containing aldehydes may be received on wine premises for use in the fermentation of wine and then returned to the distilled spirits plant...Distillates produced from one kind of fruit may not be used in the fermentation of wine made from a different kind of fruit....

2013-04-01

262

27 CFR 24.183 - Use of distillates containing aldehydes.  

Code of Federal Regulations, 2011 CFR

...containing aldehydes may be received on wine premises for use in the fermentation of wine and then returned to the distilled spirits plant...Distillates produced from one kind of fruit may not be used in the fermentation of wine made from a different kind of fruit....

2011-04-01

263

27 CFR 24.183 - Use of distillates containing aldehydes.  

...containing aldehydes may be received on wine premises for use in the fermentation of wine and then returned to the distilled spirits plant...Distillates produced from one kind of fruit may not be used in the fermentation of wine made from a different kind of fruit....

2014-04-01

264

27 CFR 19.203 - Alternation of distilled spirits plant and bonded wine cellar premises.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Alternation of distilled spirits plant and bonded wine cellar premises. 19.203...OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Qualification of Distilled Spirits Plants Alternate Operations § 19.203...

2010-04-01

265

27 CFR 19.133 - Use of distilled spirits plant premises.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Use of distilled spirits plant premises. 19.133 Section 19.133...TREASURY LIQUORS DISTILLED SPIRITS PLANTS Location and Use § 19.133 Use of distilled spirits plant premises. (a) General. No...

2010-04-01

266

27 CFR 19.204 - Alternation of distilled spirits plant and taxpaid wine bottling house premises.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Alternation of distilled spirits plant and taxpaid wine bottling house premises...OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Qualification of Distilled Spirits Plants Alternate Operations § 19.204...

2010-04-01

267

27 CFR 27.48 - Imported distilled spirits, wines, and beer.  

Code of Federal Regulations, 2010 CFR

... Imported distilled spirits, wines, and beer. Internal revenue taxes payable on imported distilled spirits, including perfumes containing distilled spirits, and on wines and beer, are collected, accounted for, and deposited as internal revenue...

2010-04-01

268

27 CFR 27.48 - Imported distilled spirits, wines, and beer.  

Code of Federal Regulations, 2011 CFR

... Imported distilled spirits, wines, and beer. Internal revenue taxes payable on imported distilled spirits, including perfumes containing distilled spirits, and on wines and beer, are collected, accounted for, and deposited as internal revenue...

2011-04-01

269

27 CFR 27.48 - Imported distilled spirits, wines, and beer.  

Code of Federal Regulations, 2012 CFR

... Imported distilled spirits, wines, and beer. Internal revenue taxes payable on imported distilled spirits, including perfumes containing distilled spirits, and on wines and beer, are collected, accounted for, and deposited as internal revenue...

2012-04-01

270

27 CFR 27.48 - Imported distilled spirits, wines, and beer.  

... Imported distilled spirits, wines, and beer. Internal revenue taxes payable on imported distilled spirits, including perfumes containing distilled spirits, and on wines and beer, are collected, accounted for, and deposited as internal revenue...

2014-04-01

271

27 CFR 27.48 - Imported distilled spirits, wines, and beer.  

Code of Federal Regulations, 2013 CFR

... Imported distilled spirits, wines, and beer. Internal revenue taxes payable on imported distilled spirits, including perfumes containing distilled spirits, and on wines and beer, are collected, accounted for, and deposited as internal revenue...

2013-04-01

272

27 CFR 19.584 - Materials for the production of distilled spirits.  

Code of Federal Regulations, 2013 CFR

...2013-04-01 false Materials for the production of distilled spirits. 19.584...TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Records and Reports Production Records § 19.584 Materials for the production of distilled spirits. A...

2013-04-01

273

27 CFR 19.584 - Materials for the production of distilled spirits.  

...2014-04-01 false Materials for the production of distilled spirits. 19.584...TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Records and Reports Production Records § 19.584 Materials for the production of distilled spirits. A...

2014-04-01

274

27 CFR 19.584 - Materials for the production of distilled spirits.  

Code of Federal Regulations, 2011 CFR

...2011-04-01 false Materials for the production of distilled spirits. 19.584...TREASURY LIQUORS DISTILLED SPIRITS PLANTS Records and Reports Production Records § 19.584 Materials for the production of distilled spirits. A...

2011-04-01

275

27 CFR 19.584 - Materials for the production of distilled spirits.  

Code of Federal Regulations, 2012 CFR

...2012-04-01 false Materials for the production of distilled spirits. 19.584...TREASURY LIQUORS DISTILLED SPIRITS PLANTS Records and Reports Production Records § 19.584 Materials for the production of distilled spirits. A...

2012-04-01

276

27 CFR 19.295 - Removal or destruction of distilling material.  

Code of Federal Regulations, 2012 CFR

...DISTILLED SPIRITS PLANTS Production of Distilled Spirits...material: (1) To plant premises, other...not involving the production of spirits, alcohol...introduced into the production system from the...distilled spirits plant or bonded...

2012-04-01

277

27 CFR 19.295 - Removal or destruction of distilling material.  

Code of Federal Regulations, 2013 CFR

...DISTILLED SPIRITS PLANTS Production of Distilled Spirits...material: (1) To plant premises, other...not involving the production of spirits, alcohol...introduced into the production system from the...distilled spirits plant or bonded...

2013-04-01

278

27 CFR 19.295 - Removal or destruction of distilling material.  

...DISTILLED SPIRITS PLANTS Production of Distilled Spirits...material: (1) To plant premises, other...not involving the production of spirits, alcohol...introduced into the production system from the...distilled spirits plant or bonded...

2014-04-01

279

27 CFR 19.295 - Removal or destruction of distilling material.  

Code of Federal Regulations, 2011 CFR

...DISTILLED SPIRITS PLANTS Production of Distilled Spirits...material: (1) To plant premises, other...not involving the production of spirits, alcohol...introduced into the production system from the...distilled spirits plant or bonded...

2011-04-01

280

27 CFR 27.61 - Containers of distilled spirits to bear closures.  

Code of Federal Regulations, 2012 CFR

... 2012-04-01 false Containers of distilled spirits to bear closures. 27.61 Section 27.61 Alcohol, Tobacco Products...Distilled Spirits § 27.61 Containers of distilled spirits to bear closures. No person shall transport, buy,...

2012-04-01

281

27 CFR 27.61 - Containers of distilled spirits to bear closures.  

... 2014-04-01 false Containers of distilled spirits to bear closures. 27.61 Section 27.61 Alcohol, Tobacco Products...Distilled Spirits § 27.61 Containers of distilled spirits to bear closures. No person shall transport, buy,...

2014-04-01

282

27 CFR 27.61 - Containers of distilled spirits to bear closures.  

Code of Federal Regulations, 2013 CFR

... 2013-04-01 false Containers of distilled spirits to bear closures. 27.61 Section 27.61 Alcohol, Tobacco Products...Distilled Spirits § 27.61 Containers of distilled spirits to bear closures. No person shall transport, buy,...

2013-04-01

283

40 CFR 417.50 - Applicability; description of the glycerine distillation subcategory.  

Code of Federal Regulations, 2010 CFR

...description of the glycerine distillation subcategory. 417.50 Section...POINT SOURCE CATEGORY Glycerine Distillation Subcategory § 417.50 Applicability...description of the glycerine distillation subcategory. The...

2010-07-01

284

27 CFR 5.47 - Standards of fill (distilled spirits bottled before January 1, 1980).  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Standards of fill (distilled spirits bottled before January 1, 1980). 5...LIQUORS LABELING AND ADVERTISING OF DISTILLED SPIRITS Standards of Fill for Bottled Distilled Spirits § 5.47 Standards of fill...

2010-04-01

285

27 CFR 27.120 - Persons authorized to receive distilled spirits imported in bulk.  

Code of Federal Regulations, 2010 CFR

... Persons authorized to receive distilled spirits imported in bulk. 27.120 Section...TREASURY LIQUORS IMPORTATION OF DISTILLED SPIRITS, WINES, AND BEER Importation of Distilled Spirits In Bulk § 27.120 Persons...

2010-04-01

286

77 FR 6038 - Revisions to Distilled Spirits Plant Operations Reports and Regulations; Comment Period Extension  

Federal Register 2010, 2011, 2012, 2013

...RIN 1513-AB89 Revisions to Distilled Spirits Plant Operations Reports and Regulations...Notice No. 124, Revisions to Distilled Spirits Plant Operations Reports and Regulations...response to a request from a distilled spirits industry association. DATES:...

2012-02-07

287

77 FR 38758 - Proposed Amendment to the Standards of Identity for Distilled Spirits; Comment Period Extension  

Federal Register 2010, 2011, 2012, 2013

...the Standards of Identity for Distilled Spirits; Comment Period Extension AGENCY: Alcohol...the Standards of Identity for Distilled Spirits, for an additional 10 days. In Notice...of identity regulations for distilled spirits to include...

2012-06-29

288

40 CFR 417.50 - Applicability; description of the glycerine distillation subcategory.  

Code of Federal Regulations, 2011 CFR

...description of the glycerine distillation subcategory. 417.50 Section...POINT SOURCE CATEGORY Glycerine Distillation Subcategory § 417.50 Applicability...description of the glycerine distillation subcategory. The...

2011-07-01

289

EFFECT OF NUTRIENT SUPPLEMENTATION OF CRUDE OR DETOXIFIED CONCENTRATED DISTILLED GRAPE MARC HEMICELLULOSIC HYDROLYSATES ON THE XYLITOL PRODUCTION BY Debaryomyces hansenii  

Microsoft Academic Search

Biosynthesis of xylitol using the yeast Debaryomyces hansenii NRRL Y-7426 was carried out using distilled grape marc (DGM) hemicellulosic hydrolysates directly concentrated by vacuum evaporation or after detoxification with activated charcoal. The effect of nutrient supplementation with vinasses, corn steep liquor (CSL) or commercial nutrients was explored. Using crude concentrated hemicellulosic hydrolysates, the maximum xylitol concentration, 11.3 g\\/L, was achieved after

José Manuel Salgado; Noelia Rodríguez; Sandra Cortés; José Manuel Domínguez

2012-01-01

290

Determination of lithium in rocks by distillation  

USGS Publications Warehouse

A method for the quantitative extraction and recovery of lithium from rocks is based on a high temperature volatilization procedure. The sample is sintered with a calcium carbonate-calcium chloride mixture at 1200?? C. for 30 minutes in a platinum ignition tube, and the volatilization product is collected in a plug of Pyrex glass wool in a connecting Pyrex tube. The distillate, which consists of the alkali chlorides with a maximum of 5 to 20 mg. of calcium oxide and traces of a few other elements, is removed from the apparatus by dissolving in dilute hydrochloric acid and subjected to standard analytiaal procedures. The sinter residues contained less than 0.0005% lithium oxide. Lithium oxide was recovered from synthetic samples with an average error of 1.1%.

Fletcher, M.H.

1949-01-01

291

ISABELLE vacuum systems  

SciTech Connect

The Intersecting Storage Accelerator (ISABELLE) consists of two rings having a circumference of 3.8 km each. In these rings superconducting magnets, held at 4 K, bend and focus the proton beam which is accelerated up to 400 GeV. Due to very different pressure requirements, ISABELLE has two completely independent vacuum systems. One, which operates at 1 x 10/sup -11/ Torr, provides a very clean environment for the circulating proton beam. Here only ion and titanium sublimation pumps are used to provide the vacuum. The other system maintains superconducting magnet vessels at a pressure below 1 x 10/sup -4/ Torr, since at this pressure the gas conduction becomes negligible. In this so-called insulating vacuum system, turbomolecular pumps pump the inadvertent small helium leaks. Other gases are cryocondensed on the cold surfaces of the cryogenic system. The basic element of ISABELLE known as Full Cell containing 45 meters of beam tube, 8 pumping stations, 8 superconducting magnets and complete instrumentation has been constructed, leak checked and tested. All design parameters have been achieved in both vacuum systems. The two vacuum systems are described with particular emphasis on the influence of superconducting magnets in the selection of materials and UHV components.

Halama, H J

1980-01-01

292

27 CFR 1.71 - Distilled spirits in containers of a capacity of one gallon or less.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 2010-04-01 false Distilled spirits in containers of a capacity of one gallon...ADMINISTRATION ACT, NONINDUSTRIAL USE OF DISTILLED SPIRITS AND WINE, BULK SALES AND BOTTLING OF DISTILLED SPIRITS Nonindustrial Use of Distilled...

2010-04-01

293

Vapor Compression Distillation Subsystem (VCDS) component enhancement, testing and expert fault diagnostics development, volume 1  

NASA Technical Reports Server (NTRS)

Vapor compression distillation technology for phase change recovery of potable water from wastewater has evolved as a technically mature approach for use aboard the Space Station. A program to parametrically test an advanced preprototype Vapor Compression Distillation Subsystem (VCDS) was completed during 1985 and 1986. In parallel with parametric testing, a hardware improvement program was initiated to test the feasibility of incorporating several key improvements into the advanced preprototype VCDS following initial parametric tests. Specific areas of improvement included long-life, self-lubricated bearings, a lightweight, highly-efficient compressor, and a long-life magnetic drive. With the exception of the self-lubricated bearings, these improvements are incorporated. The advanced preprototype VCDS was designed to reclaim 95 percent of the available wastewater at a nominal water recovery rate of 1.36 kg/h achieved at a solids concentration of 2.3 percent and 308 K condenser temperature. While this performance was maintained for the initial testing, a 300 percent improvement in water production rate with a corresponding lower specific energy was achieved following incorporation of the improvements. Testing involved the characterization of key VCDS performance factors as a function of recycle loop solids concentration, distillation unit temperature and fluids pump speed. The objective of this effort was to expand the VCDS data base to enable defining optimum performance characteristics for flight hardware development.

Kovach, L. S.; Zdankiewicz, E. M.

1987-01-01

294

Steam distillation effect and oil quality change during steam injection  

SciTech Connect

Steam distillation is an important mechanism which reduces residual oil saturation during steam injection. It may be the main recovery mechanism in steamflooding of light oil reservoirs. As light components are distilled the residual (initial) oil, the residuum becomes heavier. Mixing the distilled components with the initial oil results in a lighter produced oil. A general method has been developed to compute steam distillation yield and to quantify oil quality changes during steam injection. The quantitative results are specific because the California crude data bank was used. But general principles were followed and calculations were based on information extracted from the DOE crude oil assay data bank. It was found that steam distillation data from the literature can be correlated with the steam distillation yield obtained from the DOE crude oil assays. The common basis for comparison was the equivalent normal boiling point. Blending of distilled components with the initial oil results in API gravity changes similar to those observed in several laboratory and field operations.

Lim, K.T.; Ramey, H.J. Jr.; Brigham, W.E.

1992-01-01

295

Vacuum driven accelerated expansion  

E-print Network

It has been shown that an improved estimation of quantum vacuum energy can yield not only acceptable but also experimentally sensible results. The very idea consists in a straightforward extraction of gravitationally interacting part of the full quantum vacuum energy by means of gauge transformations. The implementation of the idea has been performed in the formalism of effective action, in the language of Schwinger's proper time and the Seeley-DeWitt heat kernel expansion, in the background of the Friedmann-Robertson-Walker geometry.

Bogus?aw Broda; Piotr Bronowski; Marcin Ostrowski; Micha? Szanecki

2008-12-29

296

Production of dl-limonene by vacuum pyrolysis of used tires  

Microsoft Academic Search

Various samples of used car and truck tires were pyrolyzed in a batch mode under vacuum and in a continuous feed reactor. The pyrolysis temperature varied in the range of 440–570°C. dl-limonene is a major product formed during the thermal decomposition of rubber under reduced pressure conditions. The pyrolysis oils were distilled to obtain a dl-limonene-rich fraction. The difficulty of

Hooshang Pakdel; Dana Magdalena Pantea; Christian Roy

2001-01-01

297

Sudden death of distillability in qutrit-qutrit systems  

E-print Network

We introduce the concept of distillability sudden death, i.e., free entangled states can evolve into non-distillable (bound entangled or separable) states in finite time under local noise. We describe the phenomenon through a specific model of local dephasing noise and compare the behavior of states in terms of the Bures fidelity. Then we propose a few methods to avoid distillability sudden death of states under (general) local dephasing noise, so that free entangled states can be robust against decoherence. Moreover, we find that bound entangled states are unstable in the limit of infinite time.

Wei Song; Lin Chen; Shi-Liang Zhu

2009-04-30

298

Reducing CO2 emissions and energy consumption of heat-integrated distillation systems.  

PubMed

Distillation systems are energy and power intensive processes and contribute significantly to the greenhouse gases emissions (e.g. carbon dioxide). Reducing CO2 emissions is an absolute necessity and expensive challenge to the chemical process industries in orderto meetthe environmental targets as agreed in the Kyoto Protocol. A simple model for the calculation of CO2 emissions from heat-integrated distillation systems is introduced, considering typical process industry utility devices such as boilers, furnaces, and turbines. Furnaces and turbines consume large quantities of fuels to provide electricity and process heats. As a result, they produce considerable amounts of CO2 gas to the atmosphere. Boilers are necessary to supply steam for heating purposes; besides, they are also significant emissions contributors. The model is used in an optimization-based approach to optimize the process conditions of an existing crude oil atmospheric tower in order to reduce its CO2 emissions and energy demands. It is also applied to generate design options to reduce the emissions from a novel internally heat-integrated distillation column (HIDiC). A gas turbine can be integrated with these distillation systems for larger emissions reduction and further energy savings. Results show that existing crude oil installations can save up to 21% in energy and 22% in emissions, when the process conditions are optimized. Additionally, by integrating a gas turbine, the total emissions can be reduced further by 48%. Internal heat-integrated columns can be a good alternative to conventional heat pump and other energy intensive close boiling mixtures separations. Energy savings can reach up to 100% with respect to reboiler heat requirements. Emissions of these configurations are cut down by up to 83%, compared to conventional units, and by 36%, with respect to heat pump alternatives. Importantly, cost savings and more profit are gained in parallel to emissions minimization. PMID:16190250

Gadalla, Mamdouh A; Olujic, Zarko; Jansens, Peter J; Jobson, Megan; Smith, Robin

2005-09-01

299

A vacuum chamber feedthrough  

NASA Technical Reports Server (NTRS)

Simple and inexpensive microwave feedthrough has been designed which transfers 130 ns, 5kV pulse into vacuum chamber. Feedthrough may be used over wide range and is adaptable to most coaxial cables, since either multistrand or single strand center conductor cable can be used.

Brown, V. D.

1973-01-01

300

Vacuum ultraviolet holography  

NASA Technical Reports Server (NTRS)

The authors report the first demonstration of holographic techniques in the vacuum ultraviolet spectral region. Holograms were produced with coherent 1182 A radiation. The holograms were recorded in polymethyl methacrylate and read out with an electron microscope. A holographic grating with a fringe spacing of 836 A was produced and far-field Fraunhofer holograms of sub-micron particles were recorded.

Bjorklund, G. C.; Harris, S. E.; Young, J. F.

1974-01-01

301

Vacuum ultraviolet holography  

NASA Technical Reports Server (NTRS)

We report the first demonstration of holographic techniques in the vacuum ultraviolet spectral region. Holograms were produced with coherent 1182-A radiation. The holograms were recorded in polymethyl methacrylate and examined with an electron microscope. A holographic grating with a fringe spacing of 386 A was produced and far-field Fraunhofer holograms of submicron particles were recorded.

Bjorklund, G. C.; Harris, S. E.; Young, J. F.

1974-01-01

302

Vacuum insulator coating development  

Microsoft Academic Search

The authors discuss the electrical and mechanical requirements for vacuum insulators in high peak power generators. To increase the lifetime of these insulators, they have developed a coating called Dendresist. This coating has extended the insulator lifetime on the PITHON, DM2, CASINO, and Double-EAGLE pulsed power generators. They describe its development, and compare its electrical and mechanical strength to that

I. S. Roth; P. S. Sincerny; L. Mandelcorn; M. Mendelsohn; D. Smith; T. G. Engel; L. Schlitt; C. M. Cooke

1997-01-01

303

On Lovelock vacuum solution  

E-print Network

We show that the asymptotic large $r$ limit of all Lovelock vacuum and electrovac solutions with $\\Lambda$ is always the Einstein solution in $d \\geq 2n+1$ dimensions. It is completely free of the order $n$ of the Lovelock polynomial indicating universal asymptotic behaviour.

Naresh Dadhich

2010-12-18

304

Process for the preparation of hydrocarbon oil distillates  

SciTech Connect

Distillates are prepared from asphaltenes-rich feeds by a process comprising subjecting the feed to solvent deasphalting, and subjecting the resulting asphaltic bitumen fraction to a combination of catalytic hydrotreating and thermal cracking.

Van Dongen, R. H.; Stork, W. H. J.

1985-02-19

305

Setting the Pressure at Which to Conduct a Distillation.  

ERIC Educational Resources Information Center

Discusses how pressure setting is determined for distillation columns, examining factors which must be considered when optimizing design for economical balance. Also discusses the basics of heat exchangers and cites a common problem with pressure differences. (JM)

Barduhn, Allen J.

1984-01-01

306

Explosion hazards in crude, distillate storage tanks assessed  

SciTech Connect

Explosion and fire hazards in crude oil and light distillate storage tanks have been assessed by actual field temperature measurements at the Zarka refinery in Jordan. Results of the assessment are presented.

Tamimi, A. (Jordan University of Science and Technology, Irbid (JO))

1990-11-19

307

Absorption Cycle Fundamentals and Applications Guidelines for Distillation Energy Savings  

E-print Network

The absorption cycle offers one of the most economic and widely applicable technologies for waste heat upgrading. It can use off-the-shelf hardware that is available now, at any required capacity rating. Fractional distillations, as a class...

Erickson, D. C.; Davidson, W. F.

1984-01-01

308

27 CFR 19.651 - Liability for distilled spirits tax.  

...DEPARTMENT OF THE TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Production of Vinegar by the Vaporizing Process Liability for...produced in, or removed from, the premises of a vinegar plant in violation of law or regulations. (26...

2014-04-01

309

27 CFR 19.651 - Liability for distilled spirits tax.  

Code of Federal Regulations, 2012 CFR

...DEPARTMENT OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Production of Vinegar by the Vaporizing Process Liability for...produced in, or removed from, the premises of a vinegar plant in violation of law or regulations. (26...

2012-04-01

310

27 CFR 19.651 - Liability for distilled spirits tax.  

Code of Federal Regulations, 2013 CFR

...DEPARTMENT OF THE TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Production of Vinegar by the Vaporizing Process Liability for...produced in, or removed from, the premises of a vinegar plant in violation of law or regulations. (26...

2013-04-01

311

27 CFR 19.651 - Liability for distilled spirits tax.  

Code of Federal Regulations, 2011 CFR

...DEPARTMENT OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Production of Vinegar by the Vaporizing Process Liability for...produced in, or removed from, the premises of a vinegar plant in violation of law or regulations. (26...

2011-04-01

312

27 CFR 19.830 - Application of distilled spirits tax.  

Code of Federal Regulations, 2010 CFR

...DEPARTMENT OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Production of Vinegar by the Vaporizing Process Administrative...produced in or removed from the premises of a vinegar plant in violation of law or this...

2010-04-01

313

Energy Efficiency in Cryogenic Fractionation Through Distributive Distillation  

E-print Network

The Advanced Recovery System (ARS) is a patented process that uses the principle of distributed distillation to achieve energy efficiency in the olefins process. This paper describes the concept of ARS and how, by integrating the chill...

Carradine, C. R.; McCue, R. H.

314

Membrane augmented distillation to separate solvents from water  

DOEpatents

Processes for removing water from organic solvents, such as ethanol. The processes include distillation to form a rectified overhead vapor, compression of the rectified vapor, and treatment of the compressed vapor by two sequential membrane separation steps.

Huang, Yu; Baker, Richard W.; Daniels, Rami; Aldajani, Tiem; Ly, Jennifer H.; Alvarez, Franklin R.; Vane, Leland M.

2012-09-11

315

Cryogenic hydrogen isotope distillation for the fusion fuel cycle  

SciTech Connect

Cryogenic distillation is an attractive method for the hydrogen isotopic separations required in fusion fuel cycles. The theoretical and practical aspects of designing and constructing such systems are well established. Practical considerations in the design of systems are presented and applied to the Isotope Separation System (ISS) at the Tritium Systems Test Assembly (TSTA), as well as systems of distillation columns that might be used for a reactor such as the Tokamak Fusion Core Experiment (TFCX) and the recovery of breeding blanket product.

Sherman, R.H.

1985-01-01

316

Comparison of cattle fecal communities from animals fed diets containing corn and distiller's grains  

Technology Transfer Automated Retrieval System (TEKTRAN)

Background and aims: Distiller’s grain is a byproduct of ethanol production, and is considered a good source of protein for cattle. However, there is concern that use of distiller’s grain may create a gastrointestinal environment that allows the growth of fecal pathogens, and the specific changes t...

317

RAPID DISTILLATION COUPLED WITH ION CHROMATOGRAPHY FOR THE DETERMINATION OF SIX ALKYLAMINES IN COSMETICS  

Microsoft Academic Search

A rapid distillation method coupled with ion chromatography was developed for simultaneous determination of methylamine, ethylamine, dimethylamine, trimethylamine, propylamine, and butylamine in cosmetics. The distillation system was designed professionally to achieve rapid distillation in less than 3 min and eliminate the interferences of alkali metals, alkaline earth and organic compounds effectively. Samples were distilled using vapour stream under alkaline conditions and

Zhixiong Zhong; Gongke Li; Binghui Zhu; Zhibin Luo

2012-01-01

318

27 CFR 1.81 - Importation of distilled spirits in bulk.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Importation of distilled spirits in bulk. 1.81 Section 1.81 Alcohol...ADMINISTRATION ACT, NONINDUSTRIAL USE OF DISTILLED SPIRITS AND WINE, BULK SALES AND BOTTLING OF DISTILLED SPIRITS Bulk Sales and Bottling of Distilled...

2010-04-01

319

27 CFR 1.80 - Sales of distilled spirits in bulk.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Sales of distilled spirits in bulk. 1.80 Section 1.80 Alcohol...ADMINISTRATION ACT, NONINDUSTRIAL USE OF DISTILLED SPIRITS AND WINE, BULK SALES AND BOTTLING OF DISTILLED SPIRITS Bulk Sales and Bottling of Distilled...

2010-04-01

320

27 CFR 28.301 - Loss of distilled spirits in transit.  

Code of Federal Regulations, 2011 CFR

...2011-04-01 2011-04-01 false Loss of distilled spirits in transit. 28.301 Section 28.301 Alcohol, Tobacco Products...Distilled Spirits § 28.301 Loss of distilled spirits in transit. The tax on distilled spirits withdrawn...

2011-04-01

321

27 CFR 28.301 - Loss of distilled spirits in transit.  

...2014-04-01 2014-04-01 false Loss of distilled spirits in transit. 28.301 Section 28.301 Alcohol, Tobacco Products...Distilled Spirits § 28.301 Loss of distilled spirits in transit. The tax on distilled spirits withdrawn...

2014-04-01

322

27 CFR 28.301 - Loss of distilled spirits in transit.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 2010-04-01 false Loss of distilled spirits in transit. 28.301 Section 28.301 Alcohol, Tobacco Products...Distilled Spirits § 28.301 Loss of distilled spirits in transit. The tax on distilled spirits withdrawn...

2010-04-01

323

27 CFR 28.301 - Loss of distilled spirits in transit.  

Code of Federal Regulations, 2012 CFR

...2012-04-01 2012-04-01 false Loss of distilled spirits in transit. 28.301 Section 28.301 Alcohol, Tobacco Products...Distilled Spirits § 28.301 Loss of distilled spirits in transit. The tax on distilled spirits withdrawn...

2012-04-01

324

27 CFR 28.301 - Loss of distilled spirits in transit.  

Code of Federal Regulations, 2013 CFR

...2013-04-01 2013-04-01 false Loss of distilled spirits in transit. 28.301 Section 28.301 Alcohol, Tobacco Products...Distilled Spirits § 28.301 Loss of distilled spirits in transit. The tax on distilled spirits withdrawn...

2013-04-01

325

A radiation hard vacuum switch  

DOEpatents

A vacuum switch with an isolated trigger probe which is not directly connected to the switching electrodes. The vacuum switch within the plasmatron is triggered by plasma expansion initiated by the trigger probe which travels through an opening to reach the vacuum switch elements. The plasma arc created is directed by the opening to the space between the anode and cathode of the vacuum switch to cause conduction. 3 figs.

Boettcher, G.E.

1988-07-19

326

Toxicity of petroleum hydrocarbon distillates to soil organisms.  

PubMed

Canadian standards for petroleum hydrocarbons in soil are based on four distillate ranges (F1, C6-C10; F2, >C10-C16; F3, >C16-C34; and F4, >C34). Concerns have arisen that the ecological soil contact standards for F3 may be overly conservative. Oil distillates were prepared and characterized, and the toxicity of F3 and two subfractions, F3a (>C16-C23) and F3b (>C23-C34), to earthworms (Eisenia andrei), springtails (Orthonychiurus folsomi), and northern wheatgrass (Elymus lanceolatus), as well as the toxicity of F2 to earthworms, was determined. Clean soil was spiked with individual distillates and measured concentrations were determined for select tests. Results agree with previous studies with these distillates. Reported toxicities of crude and petroleum products to invertebrates were generally comparable to that of F3 and F3a. The decreasing order of toxicity was F3a?>?F3?>?F3b with invertebrates, and F3a?>?F3b?>?F3 with plants. The toxicities of F3a and F3b were not sufficiently different to recommend regulating hydrocarbons based on these distillate ranges. The results also suggest that test durations may be insufficient for determining toxicity of higher distillate ranges, and that the selection of species and endpoints may significantly affect interpretation of toxicity test results. PMID:20836068

Cermak, Janet H; Stephenson, Gladys L; Birkholz, Detlef; Wang, Zhendi; Dixon, D George

2010-12-01

327

Surge-damping vacuum valve  

DOEpatents

A valve having a mechanism for damping out flow surges in a vacuum system which utilizes a slotted spring-loaded disk positioned adjacent the valve's vacuum port. Under flow surge conditions, the differential pressure forces the disk into sealing engagement with the vacuum port, thereby restricting the flow path to the slots in the disk damping out the flow surge.

Bullock, Jack C. (Pleasanton, CA); Kelly, Benjamin E. (Tracy, CA)

1980-01-01

328

Portable vacuum object handling device  

SciTech Connect

The disclosure relates to a portable device adapted to handle objects which are not to be touched by hand. A piston and bore wall form a vacuum chamber communicating with an adaptor sealably engageable with an object to be lifted. The piston is manually moved and set to establish vacuum. A valve is manually actuable to apply the vacuum to lift the object.

Anderson, G.H.

1981-07-30

329

Portable vacuum object handling device  

DOEpatents

The disclosure relates to a portable device adapted to handle objects which are not to be touched by hand. A piston and bore wall form a vacuum chamber communicating with an adaptor sealably engageable with an object to be lifted. The piston is manually moved and set to establish vacuum. A valve is manually actuatable to apply the vacuum to lift the object.

Anderson, Gordon H. (Los Alamos, NM)

1983-08-09

330

Compact vacuum insulation  

DOEpatents

An ultra-thin compact vacuum insulation panel is comprised of two hard, but bendable metal wall sheets closely spaced apart from each other and welded around the edges to enclose a vacuum chamber. Glass or ceramic spacers hold the wall sheets apart. The spacers can be discrete spherical beads or monolithic sheets of glass or ceramic webs with nodules protruding therefrom to form essentially "point" or "line" contacts with the metal wall sheets. In the case of monolithic spacers that form "line" contacts, two such spacers with the line contacts running perpendicular to each other form effectively "point" contacts at the intersections. Corrugations accommodate bending and expansion, tubular insulated pipes and conduits, and preferred applications are also included.

Benson, David K. (Golden, CO); Potter, Thomas F. (Denver, CO)

1993-01-01

331

Compact vacuum insulation embodiments  

DOEpatents

An ultra-thin compact vacuum insulation panel is comprised of two hard, but bendable metal wall sheets closely spaced apart from each other and welded around the edges to enclose a vacuum chamber. Glass or ceramic spacers hold the wall sheets apart. The spacers can be discrete spherical beads or monolithic sheets of glass or ceramic webs with nodules protruding therefrom to form essentially "point" or "line" contacts with the metal wall sheets. In the case of monolithic spacers that form "line" contacts, two such spacers with the line contacts running perpendicular to each other form effectively "point" contacts at the intersections. Corrugations accommodate bending and expansion, tubular insulated pipes and conduits, and preferred applications are also included.

Benson, David K. (Golden, CO); Potter, Thomas F. (Denver, CO)

1992-01-01

332

Compact vacuum insulation  

DOEpatents

An ultra-thin compact vacuum insulation panel is comprised of two hard, but bendable metal wall sheets closely spaced apart from each other and welded around the edges to enclose a vacuum chamber. Glass or ceramic spacers hold the wall sheets apart. The spacers can be discrete spherical beads or monolithic sheets of glass or ceramic webs with nodules protruding therefrom to form essentially point'' or line'' contacts with the metal wall sheets. In the case of monolithic spacers that form line'' contacts, two such spacers with the line contacts running perpendicular to each other form effectively point'' contacts at the intersections. Corrugations accommodate bending and expansion, tubular insulated pipes and conduits, and preferred applications are also included.

Benson, D.K.; Potter, T.F.

1993-01-05

333

Integrated structure vacuum tube  

NASA Technical Reports Server (NTRS)

High efficiency, multi-dimensional thin film vacuum tubes suitable for use in high temperature, high radiation environments are described. The tubes are fabricated by placing thin film electrode members in selected arrays on facing interior wall surfaces of an alumina substrate envelope. Cathode members are formed using thin films of triple carbonate. The photoresist used in photolithography aids in activation of the cathodes by carbonizing and reacting with the reduced carbonates when heated in vacuum during forming. The finely powdered triple carbonate is mixed with the photoresist used to delineate the cathode locations in the conventional solid state photolithographic manner. Anode and grid members are formed using thin films of refractory metal. Electron flow in the tubes is between grid elements from cathode to anode as in a conventional three-dimensional tube.

Dimeff, J.; Kerwin, W. J. (inventors)

1976-01-01

334

Vacuum tool manipulator  

DOEpatents

Apparatus for manipulating a vacuum hose in a reactor vessel comprises a housing with two opposing openings, an arm carried by the housing and deployable from a stowed position essentially completely within the housing to an extended position where the arm extends through the two openings in a generally horizontal position. The arm preferably has a two-fingered gripping device for gripping the vacuum hose but may carry a different end effector such as a grinding wheel. The fingers are opened and closed by one air cylinder. A second air cylinder extends the device. A third air cylinder within the housing pivotally pulls the opposing end of the arm into the housing via a pivoting member pivotally connected between the third air cylinder shaft and the arm.

Zollinger, William T. (3927 Almon Dr., Martinez, GA 30907)

1993-01-01

335

Vacuum tool manipulator  

DOEpatents

Apparatus for manipulating a vacuum hose in a reactor vessel comprises a housing with two opposing openings, an arm carried by the housing and deployable from a stowed position essentially completely within the housing to an extended position where the arm extends through the two openings in a generally horizontal position. The arm preferably has a two-fingered gripping device for gripping the vacuum hose but may carry a different end effector such as a grinding wheel. The fingers are opened and closed by one air cylinder. A second air cylinder extends the device. A third air cylinder within the housing pivotally pulls the opposing end of the arm into the housing via a pivoting member pivotally connected between the third air cylinder shaft and the arm. 6 figures.

Zollinger, W.T.

1993-11-23

336

The vacuum energy crisis  

E-print Network

The smallness of the vacuum energy density and its near coincidence with the average matter density of the universe are naturally explained by anthropic selection. An alternative explanation, based on the cyclic model of Steinhardt and Turok, does not address the coincidence problem and is therefore less convincing. This article appeared in ``Science'' (4 May 2006) as a ``perspective'' for Steinhardt and Turok's paper in the same issue (astro-ph/0605173).

Alexander Vilenkin

2006-05-09

337

Is vacuum dispersive?  

E-print Network

The question we ask is: does the speed of light {\\it{in vacuo}} depend on its frequency? While the answer is NO in the frame of classical physics, we point out that the opposite could be true if one takes into account the polarization of Dirac sea. We estimate the dependence of the index of refraction of vacuum + Dirac sea versus the wavelength of an incoming beam, and suggest a way to test this effect.

Yves Pomeau

2014-09-02

338

The LHC Vacuum System  

NASA Astrophysics Data System (ADS)

The Large Hadron Collider (LHC) at CERN, involves two proton storage rings with colliding beams of 7 TeV. The machine will be housed in the existing LEP tunnel and requires 16 m long superconducting bending magnets. The vacuum chamber will be the inner wall of the cryostat and hence at the temperature of the magnet cold bore, i.e. at 1.9 K and therefore a very good cryo-pump. To reduce the cryogenic power consumption, the heat load from synchrotron radiation and from the image currents in the vacuum chamber will be absorbed on a 'beam screen', which operates between 5 and 20 K, inserted in the magnet cold bore. The design pressure necessary for operation must provide a lifetime of many days and a stringent requirement comes from the power deposition in the superconducting magnet coils due to protons scattered on the residual gas which could lead to a magnet quench. Cryo-pumping of gas on the cold surfaces provides the necessary low gas densities but it must be ensured that the vapour pressure of cryo-sorbed molecules, of which H2 and He would be the most critical species, remains within acceptable limits. The room temperature sections of the LHC, specifically in the experiments, the vacuum must be stable against ion induced desorption and ISR-type 'pressure bumps'.

Gröbner, O.

1997-05-01

339

ESR vacuum system for the photon factory  

NASA Astrophysics Data System (ADS)

The vacuum system for the electron storage ring in the Photon Factory project is now under construction. In the beginning, we chose aluminum as the predominant material for the beam duct because of its cooling and forming properties, and ICF flanges for the connections because of its high reliability. These choices compelled us to employ some kind of transition material. Our tests showed that the transition between aluminum alloy (Al) and stainless steel (SUS) can be made either by using an Al-SUS clad plate (by explosion- and diffusion-bonding) or TIG welding with Ag and Ni plates in the spaces between. The vacuum system forms an elliptical ring with circumference of 187 m, and is mainly composed of three kinds of beam ducts and their pumping units. A B-type duct made of Al is installed at every bending magnet section, and has a passage for the distributed ion pump (DIP) along it inner arc wall. Q-type ducts can be classified into two kinds of straight ducts, types a and type b. Type-a duct made of Al is partially indented for the in-situ Ar discharge cleaning electrode, while type-b duct is made of SUS without any additional component. About 28 DIP units, 48 sputter ion pumps and 6 units of roughing pump will be installed around the ring. The design of the rough pumping units is in progress.

Kobayashi, Masanori; Horikoshi, Gen'ichi; Mizuno, Hajime

1980-11-01

340

Vapor Compression and Thermoelectric Heat Pump Heat Exchangers for a Condensate Distillation System: Design and Experiment  

NASA Technical Reports Server (NTRS)

Maximizing the reuse of wastewater while minimizing the use of consumables is critical in long duration space exploration. One of the more promising methods of reclaiming urine is the distillation/condensation process used in the cascade distillation system (CDS). This system accepts a mixture of urine and toxic stabilizing agents, heats it to vaporize the water and condenses and cools the resulting water vapor. The CDS wastewater flow requires heating and its condensate flow requires cooling. Performing the heating and cooling processes separately requires two separate units, each of which would require large amounts of electrical power. By heating the wastewater and cooling the condensate in a single heat pump unit, mass, volume, and power efficiencies can be obtained. The present work describes and compares two competing heat pump methodologies that meet the needs of the CDS: 1) a series of mini compressor vapor compression cycles and 2) a thermoelectric heat exchanger. In the paper, the system level requirements are outlined, the designs of the two heat pumps are described in detail, and the results of heat pump performance tests are provided. A summary is provided of the heat pump mass, volume and power trades and a selection recommendation is made.

Erickson, Lisa R.; Ungar, Eugene K.

2013-01-01

341

Vapor Compression and Thermoelectric Heat Pumps for a Cascade Distillation Subsystem: Design and Experiment  

NASA Technical Reports Server (NTRS)

Humans on a spacecraft require significant amounts of water for drinking, food, hydration, and hygiene. Maximizing the reuse of wastewater while minimizing the use of consumables is critical for long duration space exploration. One of the more promising consumable-free methods of reclaiming wastewater is the distillation/condensation process used in the Cascade Distillation Subsystem (CDS). The CDS heats wastewater to the point of vaporization then condenses and cools the resulting water vapor. The CDS wastewater flow requires heating for evaporation and the product water flow requires cooling for condensation. Performing the heating and cooling processes separately would require two separate units, each of which would demand large amounts of electrical power. Mass, volume, and power efficiencies can be obtained by heating the wastewater and cooling the condensate in a single heat pump unit. The present work describes and compares two competing heat pump methodologies that meet the needs of the CDS: 1) a series of mini compressor vapor compression cycles and 2) a thermoelectric heat exchanger. In the paper, the CDS system level requirements are outlined, the designs of the two heat pumps are described in detail, and the results of heat pump analysis and performance tests are provided. The mass, volume, and power requirement for each heat pump option is compared and the advantages and disadvantages of each system are listed.

Erickson, Lisa R.; Ungar, Eugene K.

2012-01-01

342

Distillation in microchemical systems using capillary forces and segmented flow.  

PubMed

Distillation is a ubiquitous method of separating liquid mixtures based on differences in volatility. Performing such separations in microfluidic systems is difficult because interfacial forces dominate over gravitational forces. We describe distillation in microchemical systems and present an integrated silicon device capable of separating liquid mixtures based on boiling point differences. Microfluidic distillation is realized by establishing vapor-liquid equilibrium during segmented flow. Enriched vapor in equilibrium with liquid is then separated using capillary forces, and thus enabling a single-stage distillation operation. Design criteria for operation of on-chip distillation is set forth, and the working principle demonstrated by separation of binary mixtures of 50 : 50 mol% MeOH-toluene and 50 : 50 mol% DCM-toluene at 70.0 degrees C. Analysis of vapor condensate and liquid exiting a single-stage device gave MeOH mole fractions of 0.22 +/- 0.03 (liquid) and 0.79 +/- 0.06 (vapor). Similarly, DCM mole fractions were estimated to be 0.16 +/- 0.07 (liquid) and 0.63 +/- 0.05 (vapor). These experimental results were consistent with phase equilibrium predictions. PMID:19532958

Hartman, Ryan L; Sahoo, Hemantkumar R; Yen, Bernard C; Jensen, Klavs F

2009-07-01

343

Avoiding Death by Vacuum  

NASA Astrophysics Data System (ADS)

The two-Higgs doublet model (2HDM) can have two electroweak breaking, CP-conserving, minima. The possibility arises that the minimum which corresponds to the known elementary particle spectrum is metastable, a possibility we call the "panic vacuum". We present analytical bounds on the parameters of the softly broken Peccei-Quinn 2HDM which are necessary and sufficient conditions to avoid this possibility. We also show that, for this particular model, the current LHC data already tell us that we are necessarily in the global minimum of the theory, regardless of any cosmological considerations about the lifetime of the false vacua.

Barroso, A.; Ferreira, P. M.; Ivanov, I.; Santos, R.; Silva, João P.

2013-07-01

344

What is vacuum?  

E-print Network

Vacuum can be defined with exact mathematical precision as the state which remains when a fermion, with all its special characteristics, is created out of absolutely nothing. The definition leads to a special form of relativistic quantum mechanics, which only requires the construction of a creation operator. This form of quantum mechanics is especially powerful for analytic calculation, at the same time as explaining, from first principles, many aspects of the Standard Model of particle physics. In particular, the characteristics of the weak, strong and electric interactions can be derived from the structure of the creation operator itself.

Peter Rowlands

2008-10-01

345

R&D ERL: Vacuum  

SciTech Connect

The ERL Vacuum systems are depicted in a figure. ERL has eight vacuum volumes with various sets of requirements. A summary of vacuum related requirements is provided in a table. Five of the eight volumes comprise the electron beamline. They are the 5-cell Superconducting RF Cavity, Superconducting e-gun, injection, loop and beam dump. Two vacuum regions are the individual cryostats insulating the 5-cell Superconducting RF Cavity and the Superconducting e-gun structures. The last ERL vacuum volume not shown in the schematic is the laser transport line. The beamline vacuum regions are separated by electropneumatic gate valves. The beam dump is common with loop beamline but is considered a separate volume due to geometry and requirements. Vacuum in the 5-cell SRF cavity is maintained in the {approx}10{sup -9} torr range at room temperature by two 20 l/s ion pumps and in the e-gun SRF cavity by one 60 l/s ion pump. Vacuum in the SRF cavities operated at 2{sup o}K is reduced to low 10{sup -11} torr via cryopumping of the cavity walls. The cathode of the e-gun must be protected from poisoning, which can occur if vacuum adjacent to the e-gun in the injection line exceeds 10-11 torr range in the injection warm beamline near the e-gun exit. The vacuum requirements for beam operation in the loop and beam dump are 10-9 torr range. The beamlines are evacuated from atmospheric pressure to high vacuum level with a particulate free, oil free turbomolecular pumping cart. 25 l/s shielded ion pumps distributed throughout the beamlines maintain the vacuum requirement. Due to the more demanding vacuum requirement of the injection beamline proximate to the e-gun, a vacuum bakeout of the injection beamline is required. In addition, two 200 l/s diode ion pumps and supplemental pumping provided by titanium sublimation pumps are installed in the injection line just beyond the exit of the e-gun. Due to expected gas load a similar pumping arrangement is planned for the beam dump. The cryostat vacuum thermally insulating the SRF cavities need only reduce the convective heat load such that heat loss is primarily radiation through several layers of multi-layer insulation and conductive end-losses which are contained by 5{sup o}K thermal transitions. Prior to cool down rough vacuum {approx}10{sup -5} torr range is established and maintained by a dedicated turbomolecular pump station. Cryopumping by the cold mass and heat shields reduces the insulating vacuum to 10{sup -7} torr range after cool down.

Mapes, M.; Smart, L.; Weiss, D.; Steszyn, A.; Todd, R.

2010-01-01

346

The vacuum arc centrifuge  

NASA Astrophysics Data System (ADS)

The separation of elements and isotopes by means of rotating magnetized plasma columns using a laser-triggered vacuum arc centrifuge is described. This vacuum arc centrifuge is sustained by the erosion and ionization of the cathode material, thus producing relatively pure, highly ionized, rotating plasma columns of the cathode material. Any solid metal, or mixture of metals, can be converted into plasma, and the constituent isotopes partially separated in the centrifuge, by fabricating the arc cathode out of the desired metals. The device also offers the possibility of operation with nonconducting solid elements or compounds by imbedding the desired substance in a conducting matrix. A wide variety of metals and combinations of metals were studied, ranging from C through Cu to Cd/Sn. Typical angular rotation frequencies of approx. 100,000 rad/sec were measured, with concomitant enrichments up to a factor of two for Cu 65. The device in its present form is not a viable source of partially enriched stable isotopes at a competitive cost.

Krishnan, M.; Hirshfield, J. L.

347

The LHC Vacuum System  

E-print Network

The Large Hadron Collider (LHC) at CERN, involves two proton storage rings with colliding beams of 7 TeV. The machine will be housed in the existing LEP tunnel and requires 16 m long superconducting b ending magnets. The vacuum chamber will be the inner wall of the cryostat and hence at the temperature of the magnet cold bore, i.e. at 1.9 K and therefore a very good cryopump. To reduce the cryogeni c power consumption, the heat load from synchrotron radiation and from the image currents in the vacuum chamber will be absorbed on a 'beam screen', which operates between 5 and 20 K, inserted in the magnet cold bore. The design pressure necessary for operation must provide a lifetime of several days and a further stringent requirement comes from the power deposition in the superconducting magnet coils due to protons scattered on the residual gas which could lead to a magnet quench. Cryopumping of gas on the cold surfaces provides the necessary low gas densities but it must be ensured that the vapour pressure of cr...

Gröbner, Oswald

1998-01-01

348

LHC vacuum system  

E-print Network

The Large Hadron Collider (LHC) project, now in the advanced construction phase at CERN, comprises two proton storage rings with colliding beams of 7-TeV energy. The machine is housed in the existing LEP tunnel with a circumference of 26.7 km and requires a bending magnetic field of 8.4 T with 14-m long superconducting magnets. The beam vacuum chambers comprise the inner 'cold bore' walls of the magnets. These magnets operate at 1.9 K, and thus serve as very good cryo-pumps. In order to reduce the cryogenic power consumption, both the heat load from synchrotron radiation emitted by the proton beams and the resistive power dissipation by the beam image currents have to be absorbed on a 'beam screen', which operates between 5 and 20 K and is inserted inside the vacuum chamber. The design of this beam screen represents a technological challenge in view of the numerous and often conflicting requirements and the very tight mechanical tolerances imposed. The synchrotron radiation produces strong outgassing from the...

Gröbner, Oswald

1999-01-01

349

Vacuum arc plasma mass separator  

NASA Astrophysics Data System (ADS)

The propagation of a metal plasma flow in a transport system with a curvilinear magnetic field was studied experimentally. The flow was generated by a pulsed vacuum arc discharge with a composite (W+Fe) cathode. The ion energy measurements at the transport system output showed that all ion components were accelerated up to equal energies per charge unit, about 150 eV and 320 eV in the outer and inner areas of the curved plasma flow, respectively. The spatial separation of the atoms of the cathode material was measured at the system output by x-ray fluorescence spectrometry. The ions of the lighter element (Fe) were concentrated in the inner part of the cathodic plasma flow deflected by the magnetic field while the distribution of the heavy element (W) was substantially shifted toward the outer area of the flow. The maximum mass separation efficiency reached 45, the effective value being 7.7. Such a system is promising for use in plasma technology for reprocessing spent nuclear fuel, namely for the separation of the heavy radioactive fission product from nuclear waste.

Paperny, V. L.; Krasov, V. I.; Lebedev, N. V.; Astrakchantsev, N. V.; Chernikch, A. A.

2015-02-01

350

Molluscicidal and antifungal activity of Erigeron speciosus steam distillate.  

PubMed

The steam-distilled fraction of the aerial parts of Erigeron speciosus (Lindl) DC was tested for activity against strawberry plant pathogenic fungi Botrytis cinerea Pers ex Fr, Colletotrichum acutatum Simmonds, C fragariae Brooks, C gloeosporioides (Penz) Penz & Sacc, and the intermediate host snail Planobdella trivolvis that harbors the trematode, Bolbophorus confusus, that infests and causes severe infections in pond-raised catfish in the Mississippi Delta region of the USA. Bioautography on silica TLC plates demonstrated antifungal activity in the steam distillate. Preliminary bioassays of the steam distillate indicated the presence of phytochemicals toxic to P trivolvis. The bioactive compounds methyl 2Z, 8Z-deca-2,8-diene-4,6-diynoate and its 2E, 8E isomer were isolated by bioassay-guided fractionation and chromatographic techniques and identified by 1H NMR spectroscopy. PMID:12400444

Meepagala, Kumudini M; Sturtz, George; Wise, David; Wedge, David E

2002-10-01

351

Quality Evaluation of Agricultural Distillates Using an Electronic Nose  

PubMed Central

The paper presents the application of an electronic nose instrument to fast evaluation of agricultural distillates differing in quality. The investigations were carried out using a prototype of electronic nose equipped with a set of six semiconductor sensors by FIGARO Co., an electronic circuit converting signal into digital form and a set of thermostats able to provide gradient temperature characteristics to a gas mixture. A volatile fraction of the agricultural distillate samples differing in quality was obtained by barbotage. Interpretation of the results involved three data analysis techniques: principal component analysis, single-linkage cluster analysis and cluster analysis with spheres method. The investigations prove the usefulness of the presented technique in the quality control of agricultural distillates. Optimum measurements conditions were also defined, including volumetric flow rate of carrier gas (15 L/h), thermostat temperature during the barbotage process (15 °C) and time of sensor signal acquisition from the onset of the barbotage process (60 s). PMID:24287525

Dymerski, Tomasz; G?bicki, Jacek; Wardencki, Waldemar; Namie?nik, Jacek

2013-01-01

352

A principal component analysis of transmission spectra of wine distillates  

NASA Astrophysics Data System (ADS)

A chemometric method of decomposing multidimensional data into a small-sized space, the principal component method, has been applied to the transmission spectra of vintage Moldovan wine distillates. A sample of 42 distillates aged from four to 7 years from six producers has been used to show the possibility of identifying a producer in a two-dimensional space of principal components describing 94.5% of the data-matrix dispersion. Analysis of the loads into the first two principal components has shown that, in order to measure the optical characteristics of the samples under study using only two wavelengths, it is necessary to select 380 and 540 nm, instead of the standard 420 and 520 nm, to describe the variability of the distillates by one principal component or 370 and 520 nm to describe the variability by two principal components.

Rogovaya, M. V.; Sinitsyn, G. V.; Khodasevich, M. A.

2014-11-01

353

Effect of feeding goats with distilled and non-distilled thyme leaves (Thymus zygis subp. gracilis) on milk and cheese properties.  

PubMed

The aim of this study was to evaluate the effect of feeding goats with distilled and non-distilled thyme leaves (Thymus zygis subsp. gracilis) on the physicochemical composition and technological properties of pasteurised goat milk, and on the physicochemical composition, phenolic content, oxidative stability, microbiology, sensory and texture profile of Murcia al Vino goat cheese. One group of goats was fed the basal diet (control), the second and third groups were fed with different levels of distilled (10 and 20%) or non-distilled (3·75 and 7·5%) thyme leaves. Goat milk physicochemical composition was significantly affected by the substitution of 7·5% of basal goat diet with non-distilled thyme leaves (increase in fat, protein, dry matter and PUFA content), while goat milk clotting time was increased significantly by the introduction of 20% distilled thyme leaves, which reduces its technological suitability. Microbiology, sensory and texture profiles were not affected by the introduction of distilled thyme leaves. The introduction of distilled and non-distilled thyme leaves as an alternative feed to diet can lead to an inhibition of lipids oxidation. The introduction of distilled and non-distilled thyme leaves into goat's diet can be successfully adopted as a strategy to reduce feeding costs and to take advantage of the waste from the production of essential oils, minimising waste removing costs and the environmental impact. PMID:24124730

Boutoial, Khalid; García, Victor; Rovira, Silvia; Ferrandini, Eduardo; Abdelkhalek, Oussama; López, María Belén

2013-11-01

354

Vacuum disconnectors an application study  

Microsoft Academic Search

The ageing of vacuum interrupters with combined functions of disconnector and circuit-breaker or switch is studied for compact shielded solid insulated switchgear. Different prototypes are manufactured to investigate the influence of contact materials and contact designs. A test program is presented that realistically represents the ageing as described in the standards. The feasibility to create vacuum disconnecting circuit-breakers, vacuum switch-disconnectors

H. Schellekens; T. Shioiri; M. Homma; P. Picot; K. Sasage; D. Mazzucchi

2010-01-01

355

Portable vacuum object handling device  

DOEpatents

The disclosure relates to a portable device adapted to handle objects which are not to be touched by hand. A piston and bore wall form a vacuum chamber communicating with an adaptor sealably engageable with an object to be lifted. The piston is manually moved and set to establish vacuum. A valve is manually actuatable to apply the vacuum to lift the object. 1 fig.

Anderson, G.H.

1983-08-09

356

Low partial discharge vacuum feedthrough  

NASA Technical Reports Server (NTRS)

Relatively discharge free vacuum feedthrough uses silver-plated copper conductor jacketed by carbon filled silicon semiconductor to reduce concentrated electric fields and minimize occurrence of partial discharge.

Benham, J. W.; Peck, S. R.

1979-01-01

357

Vacuum insulation on the moon  

NASA Astrophysics Data System (ADS)

This paper presents recent concepts and analysis on vacuum insulation issues in the lunar environment, including dust initiated breakdown, thermal management, gas contamination, and solar radiation effects.

Gordon, Lloyd B.; Gaustad, Krista L.

1994-05-01

358

Distillation and Dehydro Reactors Advanced Process Conrol Freeport Texas PLant  

E-print Network

Distillation APC – Control Matrix 6/2/2014 INTERNAL; CONFIDENTIAL 5 ESL-IE-14-05-16 Proceedings of the Thrity-Sixth Industrial Energy Technology Conference New Orleans, LA. May 20-23, 2014 G-KTI, Polyamide and Intermediates Distillation APC – Graphics Screen... Independent and Dependent Variables with Limits 6/2/2014 INTERNAL; CONFIDENTIAL 6 • The independent and dependent variables are displayed on graphics screens. • The limits of the variables are shown as pink shaded areas. • The actual value of a variable...

Eisele, D.

2014-01-01

359

Sudden death of distillability in qutrit-qutrit systems  

SciTech Connect

We introduce the concept of distillability sudden death, i.e., free entangled states can evolve into nondistillable (bound entangled or separable) states in finite time under local noise. We describe the phenomenon through a specific model of local dephasing noise and compare the behavior of states in terms of the Bures fidelity. Then we propose a few methods to avoid distillability sudden death of states under (general) local dephasing noise so that free entangled states can be robust against decoherence. Moreover, we find that bound entangled states are unstable in the limit of infinite time.

Song Wei; Zhu Shiliang [Laboratory of Quantum Information Technology, ICMP and SPTE, South China Normal University, Guangzhou 510006 (China); Chen Lin [Centre for Quantum Technologies, National University of Singapore, 3 Science Drive 2, Singapore 117542 (Singapore)

2009-07-15

360

Noisy Preprocessing and the Distillation of Private States  

E-print Network

We provide a simple security proof for prepare & measure quantum key distribution protocols employing noisy processing and one-way postprocessing of the key. This is achieved by showing that the security of such a protocol is equivalent to that of an associated key distribution protocol in which, instead of the usual maximally-entangled states, a more general {\\em private state} is distilled. Besides a more general target state, the usual entanglement distillation tools are employed (in particular, Calderbank-Shor-Steane (CSS)-like codes), with the crucial difference that noisy processing allows some phase errors to be left uncorrected without compromising the privacy of the key.

Joseph M. Renes; Graeme Smith

2006-03-28

361

Nearly Seamless Vacuum-Insulated Boxes  

NASA Technical Reports Server (NTRS)

A design concept, and a fabrication process that would implement the design concept, have been proposed for nearly seamless vacuum-insulated boxes that could be the main structural components of a variety of controlled-temperature containers, including common household refrigerators and insulating containers for shipping foods. In a typical case, a vacuum-insulated box would be shaped like a rectangular parallelepiped conventional refrigerator box having five fully closed sides and a hinged door on the sixth side. Although it is possible to construct the five-closed-side portion of the box as an assembly of five unitary vacuum-insulated panels, it is not desirable to do so because the relatively high thermal conductances of the seams between the panels would contribute significant amounts of heat leakage, relative to the leakage through the panels themselves. In contrast, the proposal would make it possible to reduce heat leakage by constructing the five-closed-side portion of the box plus the stationary portion (if any) of the sixth side as a single, seamless unit; the only remaining seam would be the edge seal around the door. The basic cross-sectional configuration of each side of a vacuum-insulated box according to the proposal would be that of a conventional vacuum-insulated panel: a low-density, porous core material filling a partially evacuated space between face sheets. However, neither the face sheets nor the core would be conventional. The face sheets would be opposite sides of a vacuum bag. The core material would be a flexible polymer-modified silica aerogel of the type described in Silica/Polymer and Silica/Polymer/Fiber Composite Aero - gels (MSC-23736) in this issue of NASA Tech Briefs. As noted in that article, the stiffness of this core material against compression is greater than that of prior aerogels. This is an important advantage because it translates to greater retention of thickness and, hence, of insulation performance when pressure is applied across the thickness, in particular, when the space between the face sheets is evacuated, causing the core material to be squeezed between the face sheets by atmospheric pressure. Fabrication of a typical vacuum-insulated box according to the proposal would begin with fabrication of a cross-shaped polymer-modified aerogel blanket. The dimensions of the cross would be chosen so that (1) the central rectangular portion of the cross would form the core for the back of the box and (2) the arms of the cross could be folded 90 from the back plane to form the cores of the adjacent four sides of the box. Optionally, the blanket could include tabs for joining the folded sides of the blanket along mating edges and tabs that could serve as hinges for the door. Vacuum bags in the form of similar five-sided boxes would be made of a suitable polymeric film, one bag to fit the outer core surface, the other to fit the inner core surface. By use of commercially available film-sealing equipment, these box-shaped bags would be seamed together to form a single vacuum bag encasing the box-shaped core. Also, a one-way valve would be sealed to the bag. Through this valve, the interior of the bag would be evacuated to a pressure between 1 and 10 torr (approximately between 0.13 and 1.3 kPa). The polymer-modified aerogel core material is known to perform well as a thermal insulator in such a partial vacuum.

Stepanian, Christopher J.; Ou, Danny; Hu, Xiangjun

2010-01-01

362

Entrapment Type Vacuum Pumps  

NSDL National Science Digital Library

This is a description for a learning module from Maricopa Advanced Technology Education Center. This PDF describes the module; access may be purchased by visiting the MATEC website. Entrapment type pumps operate primarily in the high to ultra-high vacuum ranges. The discussion in this MATEC module includes applications, theory of operation, operating range and preventative maintenance. The focus is on three major types of pumps: cryosorption, cryogenic and sputter-ion. The overall performance of these types of pumps depends on a variety of parameters. For example, it is important that learners understand the balance between pumping speed and capacity. Competency is demonstrated as the learners specify systems for defined process applications.

363

Control Dewar Secondary Vacuum Container  

SciTech Connect

This engineering note provides background information regarding the control dewar secondary vacuum container. The secondary vacuum container has it's origin with the CDP control dewar design. The name secondary vacuum container replaced the CDP term 'Watt can' which was named after Bob Watt (SLAC), a PAC/DOE review committee member who participated in a review of CDP and recommended a secondary vacuum enclosure. One of the most fragile parts of the control dewar design is the ceramic electrical feed throughs located in the secondary vacuum container. The secondary vacuum container is provided to guard against potential leaks in these ceramic insulating feed throughs. The secondary vacuum container has a pumping line separate from the main solenoid/control dewar insulating vacuum. This pumping line is connected to the inlet of the turbo pump for initial pumpdown. Under normal operation the container is isolated. Should a feedthrough develop a small leak, alternate pumping arrangements for the secondary vacuum container could be arranged. The pressure in the secondary vacuum container should be kept in a range that the breakdown voltage is kept at a maximum. The breakdown voltage is known to be a function of pressure and is described by a Paschen curve. I cannot find a copy of the curve at this time, but from what I remember, the breakdown voltage is a minimum somewhere around 10-3 torr. Ideally the pressure in the secondary vacuum can should be kept very low, around 10 E-6 or 10 E-7 torr for maximum breakdown voltage. If however a leak developed and this was not possible, then one could operate at a pressure higher than the minima point.

Rucinski, R.; /Fermilab

1993-10-04

364

Electronic-type vacuum gauges with replaceable elements  

DOEpatents

In electronic devices for measuring pressures in vacuum systems, the metal elements which undergo thermal deterioration are made readily replaceable by making them parts of a simple plug-in unit. Thus, in ionization gauges, the filament and grid or electron collector are mounted on the novel plug-in unit. In thermocouple pressure gauges, the heater and attached thermocouple are mounted on the plug-in unit. Plug-in units have been designed to function, alternatively, as ionization gauge and as thermocouple gauge, thus providing new gauges capable of measuring broader pressure ranges than is possible with either an ionization gauge or a thermocouple gauge.

Edwards, Jr., David (7 Brown's La., Bellport, NY 11713)

1984-01-01

365

Electronic-type vacuum gauges with replaceable elements  

DOEpatents

In electronic devices for measuring pressures in vacuum systems, the metal elements which undergo thermal deterioration are made readily replaceable by making them parts of a simple plug-in unit. Thus, in ionization gauges, the filament and grid or electron collector are mounted on the novel plug-in unit. In thermocouple pressure gauges, the heater and attached thermocouple are mounted on the plug-in unit. Plug-in units have been designed to function, alternatively, as ionization gauge and as thermocouple gauge, thus providing new gauges capable of measuring broader pressure ranges than is possible with either an ionization gauge or a thermocouple gauge. 5 figs.

Edwards, D. Jr.

1984-09-18

366

27 CFR 19.538 - Withdrawal of spirits by the United States.  

Code of Federal Regulations, 2010 CFR

... 2010-04-01 false Withdrawal of spirits by the United States. 19.538 Section...DEPARTMENT OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Transfer and Withdrawals Withdrawal of Spirits Free of Tax § 19.538 Withdrawal...

2010-04-01

367

Dried distillers grains with solubles in laying hen diets.  

PubMed

A study was conducted to test the inclusion rate of corn dried distillers grains with solubles (DDGS) in laying hen diets on egg production (EP) responses for a full production cycle. A total of 288 Bovan Single Comb White Leghorn laying hens were fed diets containing 0, 5, 10, 15, 20, or 25% DDGS from 24 to 46 wk (phase 1) and 47 to 76 wk (phase 2) of age. The diets were formulated to be isocaloric at 2,775 and 2,816 kcal/kg of ME and isonitrogenous at 16.5 and 16.0% CP for phases 1 and 2, respectively. Nutrient retention of both N and P were determined by the indicator methods during phase 2. Diets were replicated with 8 pens/treatment and 6 hens/pen in an unbalanced randomized complete block design. Average daily feed intake, EP, and overall weight gain were similar (P = 0.08 to 0.1) among treatments during the study. Egg weight was affected (P = 0.064) by DDGS treatment during phase 1. Hens fed 0, 5, 10, 15, 20, or 25% DDGS had an average egg weight of 60.6, 60.4, 60.8, 60.0, 59.0, and 59.0 g, respectively; however, no differences were detected in egg weight during phase 2. During phase 1, diets were formulated based on TSAA, allowing Met to decrease as DDGS increased, but during phase 2, diets were formulated to keep Met equal across DDGS treatments, allowing TSAA to increase as a result of high Cys in DDGS. Yolk color increased with increasing DDGS level; the highest Roche score (P = 0.001) was 7.2 for hens fed 25% DDGS. Nitrogen and P retention was greater (P = 0.003) in hens fed 25% DDGS. Also, N and P excretion decreased (P = 0.007) linearly as DDGS increased. In summary, feeding DDGS up to 25% during EP cycles had no negative effects on feed intake, EP, Haugh units, or specific gravity, and improved yolk color at the highest levels. Increasing DDGS level beyond 15% caused a reduction in egg weight during phase 1 of egg production, though no differences were observed in egg weight during phase 2. Nitrogen and P excretion were lower at higher inclusion rate of DDGS. Hens fed 25% DDGS had the highest N and P retention. PMID:21844261

Masa'deh, M K; Purdum, S E; Hanford, K J

2011-09-01

368

27 CFR 19.207 - Alternate use of distilled spirits plant and volatile fruit-flavor concentrate premises.  

Code of Federal Regulations, 2010 CFR

... false Alternate use of distilled spirits plant and volatile fruit-flavor concentrate premises...OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Qualification of Distilled Spirits Plants Alternate Operations § 19.207...

2010-04-01

369

40 CFR 721.7020 - Distillates (petroleum), C(3-6), polymers with styrene and mixed terpenes (generic name).  

Code of Federal Regulations, 2012 CFR

...2012-07-01 false Distillates (petroleum), C(3-6), polymers with styrene...Substances § 721.7020 Distillates (petroleum), C(3-6), polymers with styrene...The chemical substance distillates (petroleum), C(3-6), polymers with...

2012-07-01

370

40 CFR 721.7020 - Distillates (petroleum), C(3-6), polymers with styrene and mixed terpenes (generic name).  

Code of Federal Regulations, 2013 CFR

...2013-07-01 false Distillates (petroleum), C(3-6), polymers with styrene...Substances § 721.7020 Distillates (petroleum), C(3-6), polymers with styrene...The chemical substance distillates (petroleum), C(3-6), polymers with...

2013-07-01

371

40 CFR 721.7020 - Distillates (petroleum), C(3-6), polymers with styrene and mixed terpenes (generic name).  

...2014-07-01 false Distillates (petroleum), C(3-6), polymers with styrene...Substances § 721.7020 Distillates (petroleum), C(3-6), polymers with styrene...The chemical substance distillates (petroleum), C(3-6), polymers with...

2014-07-01

372

27 CFR 5.47a - Metric standards of fill (distilled spirits bottled after December 31, 1979).  

...2014-04-01 2014-04-01 false Metric standards of fill (distilled spirits...Bottled Distilled Spirits § 5.47a Metric standards of fill (distilled spirits...uniform capacity. (3) Discrepancies in measure due to differences in...

2014-04-01

373

27 CFR 5.47a - Metric standards of fill (distilled spirits bottled after December 31, 1979).  

Code of Federal Regulations, 2011 CFR

...2011-04-01 2011-04-01 false Metric standards of fill (distilled spirits...Bottled Distilled Spirits § 5.47a Metric standards of fill (distilled spirits...uniform capacity. (3) Discrepancies in measure due to differences in...

2011-04-01

374

27 CFR 5.47a - Metric standards of fill (distilled spirits bottled after December 31, 1979).  

Code of Federal Regulations, 2012 CFR

...2012-04-01 2012-04-01 false Metric standards of fill (distilled spirits...Bottled Distilled Spirits § 5.47a Metric standards of fill (distilled spirits...uniform capacity. (3) Discrepancies in measure due to differences in...

2012-04-01

375

27 CFR 5.47a - Metric standards of fill (distilled spirits bottled after December 31, 1979).  

Code of Federal Regulations, 2010 CFR

...2010-04-01 2010-04-01 false Metric standards of fill (distilled spirits...Bottled Distilled Spirits § 5.47a Metric standards of fill (distilled spirits...uniform capacity. (3) Discrepancies in measure due to differences in...

2010-04-01

376

27 CFR 5.47a - Metric standards of fill (distilled spirits bottled after December 31, 1979).  

Code of Federal Regulations, 2013 CFR

...2013-04-01 2013-04-01 false Metric standards of fill (distilled spirits...Bottled Distilled Spirits § 5.47a Metric standards of fill (distilled spirits...uniform capacity. (3) Discrepancies in measure due to differences in...

2013-04-01

377

41 CFR 102-41.205 - Do we report all forfeited distilled spirits, wine, and beer to GSA for disposal?  

Code of Federal Regulations, 2010 CFR

...Do we report all forfeited distilled spirits, wine, and beer to GSA for disposal...Special Handling Forfeited Distilled Spirits, Wine, and Beer § 102-41.205 Do we report all forfeited distilled spirits, wine, and beer to GSA for...

2010-07-01

378

19 CFR 11.7 - Distilled spirits and other alcoholic beverages imported in bottles and similar containers...  

Code of Federal Regulations, 2010 CFR

...Distilled spirits and other alcoholic beverages imported in bottles and similar containers...Distilled spirits and other alcoholic beverages imported in bottles and similar containers...distilled spirits and other alcoholic beverages in bottles and similar...

2010-04-01

379

Vacuum Gas Tungsten Arc Welding  

NASA Technical Reports Server (NTRS)

A two-year program investigated vacuum gas tungsten arc welding (VGTAW) as a method to modify or improve the weldability of normally difficult-to-weld materials. After a vacuum chamber and GTAW power supply were modified, several difficult-to-weld materials were studied and key parameters developed. Finally, Incoloy 903 weld overlays were produced without microfissures.

Weeks, J. L.; Todd, D. T.; Wooten, J. R.

1997-01-01

380

Braneworld dynamics with vacuum polarization  

E-print Network

We investigate the cosmological dynamics of a brane Universe when quantum corrections from vacuum polarization are taken into account. New vacuum de Sitter points existing on Randall-Sundrum brane are described. We show also that quantum correction can destroy the DGP de Sitter solution on induced gravity brane.

A. V. Toporensky; P. V. Tretyakov

2005-12-15

381

Vacuum Enhanced Cutaneous Biopsy Instrument  

SciTech Connect

A syringe-like disposable cutaneous biopsy instrument equipped with a tubular blade at its lower end, and designed so that a vacuum is created during use, said vacuum serving to retain undeformed a plug of tissue cut from a patient's skin.

Collins, Joseph

1999-06-25

382

Detecting leaks in vacuum bags  

NASA Technical Reports Server (NTRS)

Small leaks in vacuum bag can be readily detected by eye, using simple chemical reaction: combination of ammonia and acetic acid vapors to produce cloudy white smoke. Technique has been successfully used to test seam integrity and to identify minute pinholes in vacuum bag used in assembly of ceramic-tile heat shield for Space Shuttle Orbiter.

Carlstrom, E. E.

1980-01-01

383

Vacuum flash evaporated polymer composites  

DOEpatents

A method for fabrication of polymer composite layers in a vacuum is disclosed. More specifically, the method of dissolving salts in a monomer solution, vacuum flash evaporating the solution, condensing the flash evaporated solution as a liquid film, and forming the condensed liquid film into a polymer composite layer on a substrate is disclosed.

Affinito, J.D.; Gross, M.E.

1997-10-28

384

On simplicity of vacuum modules  

Microsoft Academic Search

We find necessary and sufficient conditions of irreducibility of vacuum modules over affine Lie algebras and superalgebras. From this we derive conditions of simplicity of minimal W-algebras. Moreover, in the case of the Virasoro and Neveu–Schwarz algebras we obtain explicit formulas for the vacuum determinants.

Maria Gorelik; Victor Kac

2007-01-01

385

Statistical mechanics of the vacuum  

E-print Network

The vacuum is full of virtual particles which exist for short moments of time. In this paper we construct a chaotic model of vacuum fluctuations associated with a fundamental entropic field that generates an arrow of time. The dynamics can be physically interpreted in terms of fluctuating virtual momenta. This model leads to a generalized statistical mechanics that distinguishes fundamental constants of nature.

Christian Beck

2011-12-07

386

Vacuum enhanced cutaneous biopsy instrument  

DOEpatents

A syringe-like disposable cutaneous biopsy instrument equipped with a tubular blade at its lower end, and designed so that a vacuum is created during use, said vacuum serving to retain undeformed a plug of tissue cut from a patient's skin.

Collins, Joseph (St. Petersburg, FL)

2000-01-01

387

??????????????????????????????????????????? Vacuum Cooling Process of Lettuce  

Microsoft Academic Search

The aim of this research work is to study the moisture and the temperature variation of lettuce under vacuum cooling processes. The experiment was carried out in a rectangular vacuum chamber having a volume of 0.036 m3. The experimental results showed that the cooling rate at the first stage of running was considerably high. the chamber temperature profile during the

Phanlop Saranyachoet; Naris Pratinthong; Thanit Swasdisevi

388

27 CFR 19.98 - Conveyance of untaxpaid spirits or wines within a distilled spirits plant.  

Code of Federal Regulations, 2010 CFR

...spirits or wines within a distilled spirits plant. 19.98 Section 19.98 Alcohol...TREASURY LIQUORS DISTILLED SPIRITS PLANTS Administrative and Miscellaneous Provisions Conveyance of Spirits Or Wines on Plant Premises § 19.98 Conveyance of...

2010-04-01

389

27 CFR 19.59 - Conveyance of untaxpaid spirits or wines within a distilled spirits plant.  

...spirits or wines within a distilled spirits plant. 19.59 Section 19.59 Alcohol...THE TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants Conveyance of Spirits Or Wines on...

2014-04-01

390

27 CFR 19.59 - Conveyance of untaxpaid spirits or wines within a distilled spirits plant.  

Code of Federal Regulations, 2011 CFR

...spirits or wines within a distilled spirits plant. 19.59 Section 19.59 Alcohol...THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants Conveyance of Spirits Or Wines on...

2011-04-01

391

27 CFR 19.59 - Conveyance of untaxpaid spirits or wines within a distilled spirits plant.  

Code of Federal Regulations, 2012 CFR

...spirits or wines within a distilled spirits plant. 19.59 Section 19.59 Alcohol...THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants Conveyance of Spirits Or Wines on...

2012-04-01

392

27 CFR 19.54 - Use of distilled spirits plant premises.  

...2014-04-01 false Use of distilled spirits plant premises. 19.54 Section 19.54...THE TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants Rules for Location and Use of A Dsp...

2014-04-01

393

27 CFR 19.51 - Home production of distilled spirits prohibited.  

...AND TRADE BUREAU, DEPARTMENT OF THE TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants § 19.51 Home production of distilled spirits prohibited. A person may not produce...

2014-04-01

394

27 CFR 19.51 - Home production of distilled spirits prohibited.  

Code of Federal Regulations, 2013 CFR

...AND TRADE BUREAU, DEPARTMENT OF THE TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants § 19.51 Home production of distilled spirits prohibited. A person may not produce...

2013-04-01

395

27 CFR 19.54 - Use of distilled spirits plant premises.  

Code of Federal Regulations, 2013 CFR

...2013-04-01 false Use of distilled spirits plant premises. 19.54 Section 19.54...THE TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants Rules for Location and Use of A Dsp...

2013-04-01

396

27 CFR 19.51 - Home production of distilled spirits prohibited.  

Code of Federal Regulations, 2012 CFR

...AND TRADE BUREAU, DEPARTMENT OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants § 19.51 Home production of distilled spirits prohibited. A person may not produce...

2012-04-01

397

27 CFR 19.54 - Use of distilled spirits plant premises.  

Code of Federal Regulations, 2011 CFR

...2011-04-01 false Use of distilled spirits plant premises. 19.54 Section 19.54...THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants Rules for Location and Use of A Dsp...

2011-04-01

398

27 CFR 19.51 - Home production of distilled spirits prohibited.  

Code of Federal Regulations, 2011 CFR

...AND TRADE BUREAU, DEPARTMENT OF THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants § 19.51 Home production of distilled spirits prohibited. A person may not produce...

2011-04-01

399

27 CFR 19.54 - Use of distilled spirits plant premises.  

Code of Federal Regulations, 2012 CFR

...2012-04-01 false Use of distilled spirits plant premises. 19.54 Section 19.54...THE TREASURY LIQUORS DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants Rules for Location and Use of A Dsp...

2012-04-01

400

27 CFR 19.315 - Removal or destruction of distilling material.  

Code of Federal Regulations, 2010 CFR

...DISTILLED SPIRITS PLANTS Production § 19.315 ...material—(a) to plant premises, other...not involving the production of (1) spirits...introduced into the production system may be...distilled spirits plant or bonded...

2010-04-01

401

27 CFR 19.59 - Conveyance of untaxpaid spirits or wines within a distilled spirits plant.  

Code of Federal Regulations, 2013 CFR

...spirits or wines within a distilled spirits plant. 19.59 Section 19.59 Alcohol...THE TREASURY ALCOHOL DISTILLED SPIRITS PLANTS Restrictions on Production, Location, and Use of Plants Conveyance of Spirits Or Wines on...

2013-04-01

402

Tomato yield responses to soil-incorporated dried distillers grains  

Technology Transfer Automated Retrieval System (TEKTRAN)

Dried distiller's grains (DDGs) are a coproduct of dry-grind corn ethanol production, most of which are used for animal feed, and are sold for under $150/metric ton. Developing higher-value uses for DDGs can increase the profitability of corn-based ethanol. Although DDGs applied directly to a pott...

403

The influence of distilled water on the fluidity of protoplasm  

Microsoft Academic Search

Summary It is found that if distilled water is allowed to flow through the leaves of terrestrial plants (Achillea millefolium, Chenopodium album, Rumex acetosella, Ficaria verna), the protoplasm of the cells exhibits increased fluidity. The terrestrial plants thus react in the same way as the earlier investigatedHelodea. The cause is not the absence of nutrient salts or of microelements, since

M. G. Stålfelt

1957-01-01

404

Solar Ethanol Distillation Oara Neumann,1,3  

E-print Network

in boiling point, the more volatile component is preferentially vaporized by the solar- illuminated particles vaporization process: the solar-illuminated particles rise to temperatures well above the boiling points environment with laser excitation to avoid vapor water contamination. This results in a distillate greatly

405

Chapter 4 Desalination: Reverse Osmosis and Membrane Distillation  

Microsoft Academic Search

Reverse osmosis (RO) and membrane distillation (MD), the two important applications associated with membrane-based desalination, are discussed in detail. Various RO process parameters, such as membrane synthesis, materials involved, and fouling control, play vital roles in the success of membrane filtration. The membrane synthesis process has a large influence on the physical and mechanical properties of the membrane. It also

Tilak Gullinkala; Brett Digman; Colleen Gorey; Richard Hausman; Isabel C. Escobar

2010-01-01

406

Distilling Free-Form Natural Laws from Experimental Data  

E-print Network

Distilling Free-Form Natural Laws from Experimental Data Michael Schmidt1 and Hod Lipson2 phenomena in nature. Despite the prevalence of computing power, the process of finding natural laws and invariants underlie nearly all physical laws in na- ture (1), suggesting that the search for many natural

Fernandez, Thomas

407

Instrumentation for potentiostatic corrosion studies with distilled water  

NASA Technical Reports Server (NTRS)

Corrosion is studied potentiostatically in the corroding environment of distilled water with an instrument that measures the potential of the corroding specimen immediately after interruption of the polarizing current. No current is flowing. The process permits compensation for IR drops when potentiostatic control is used in high resistance systems.

Loess, R. E.; Youngdahl, C. A.

1969-01-01

408

Optimal distillation of three-qubit W states  

SciTech Connect

Some of the asymmetric three-qubit W states are used for perfect teleportation, superdense coding, and quantum-information splitting. We present the protocols for the optimal distillation of the asymmetric as well as the symmetric W states from a single copy of any three-qubit W class pure state.

Yildiz, Ali [Department of Physics, Istanbul Technical University, Maslak 34469, Istanbul (Turkey)

2010-07-15

409

ALGAL BIOASSAYS WITH LEACHATES AND DISTILLATES FROM WESTERN COAL  

EPA Science Inventory

The objective of this research was to assess the effects on freshwater algae of materials derived from coal storage piles. Coal leachates and distillates were prepared in the laboratory from low-sulfur Montana coal. Three types of algal bioassays were conducted: (1) A laboratory ...

410

Novel configurations of solar distillation system for potable water production  

NASA Astrophysics Data System (ADS)

More and more surface water are polluted with toxic chemicals. Alternatively brackish and saline water are used as feed water to water treatment plants. Expensive desalination process via reverse osmosis or distillation is used in the plants. Thus, this conventional desalination is not suitable for low and medium income countries. A cheaper method is by solar distillation. However the rate of water production by this method is generally considered low. This research attempts to enhance water production of solar distillation by optimizing solar capture, evaporation and condensation processes. Solar radiation data was captured in several days in Perak, Malaysia. Three kinds of experiments were done by fabricating triangular solar distillation systems. First type was conventional solar still, second type was combined with 50 Watt solar photovoltaic panel and 40 Watt Dc heater, while third type was integrated with 12 Volt Solar battery and 40 Watt Dc heater. The present investigation showed that the productivity of second and third systems were 150% and 480% of the conventional still type, respectively. The finding of this research can be expected to have wide application in water supply particularly in areas where fresh surface water is limited.

Riahi, A.; Yusof, K. W.; Sapari, N.; Singh, B. S.; Hashim, A. M.

2013-06-01

411

Insoluble distillers' dried grain (DDG) fraction in chemically leavened bread  

Technology Transfer Automated Retrieval System (TEKTRAN)

The objective of this study was to evaluate the addition of thermo-mechanically treated corn Distillers’ Dried Grain (DDG) on batter and bread quality characteristics. DDG was processed by jet-cooking homogenized slurry of DDG and water followed by centrifugation and drum drying the insoluble fract...

412

Corn Distillers Dried Grains with Solubles (DDGS): Opportunities and Challenges  

Technology Transfer Automated Retrieval System (TEKTRAN)

Corn-based ethanol in the U.S. has dramatically increased in recent years; so has the quantity of associated coproducts. Nonfermentable components are removed from the process as whole stillage, centrifuged to remove water – which is then evaporated to produce condensed distillers solubles (CDS), a...

413

Fractional Distillation of Air and Other Demonstrations with Condensed Gases  

ERIC Educational Resources Information Center

The learning objectives of the fractional distillation of air and other demonstrations includes observing N2, O2, CO2 and H2O in air, studying the fractional separation of components based on boiling point differences and so on. The materials, reagent and equipment preparation, experimental procedures, hazards of the demonstration are also…

Oliver-Hoyo, Maria; Switzer, William L., III; Eierman, Robert

2005-01-01

414

Distilling angular momentum nonclassical states in trapped ions  

SciTech Connect

In the spirit of quantum nondemolition measurements, we show that by exploiting suitable vibronic couplings and repeatedly measuring the atomic population of a confined ion, it is possible to distill center-of-mass vibrational states with a well-defined square of angular momentum or, alternatively, angular momentum projection Schroedinger cat states.

Militello, B.; Messina, A. [INFM, MIUR, and Dipartimento di Scienze Fisiche ed Astronomiche dell'Universita di Palermo, Via Archirafi, 36, I-90123 Palermo (Italy)

2004-09-01

415

[Production of antitumor substances from shochu distillation remnants].  

PubMed

This study aimed to develop a new processing method for the effective use of rice shochu distillation remnants. We examined the inhibitory effects on the growth of human lung carcinoma cells in the medium of rice shochu distillation remnants with various fungi. Interestingly, high inhibitory effects on the growth of human lung carcinoma cells in the medium of rice shochu distillation remnants with Aspergillus oryzae were obtained, although no inhibitory effect was observed in the case of synthetic medium. We therefore fractionated the medium of rice shochu distillation remnants with A. oryzae using anion-exchange and reverse-phase chromatography. Furthermore, we attempted to determine the chemical structure of compounds that showed high inhibitory effects on the growth of tumor cells. The chemical structure of 1-hydroxy-6-(1-methylpropyl)-3-(2-methylproryl)-2(1H)-pyrazinone was revealed on the basis of liquid and gas mass spectroscopies. This compound should be completely safe based on toxic test results using model mice. PMID:16679744

Tsuchiya, Kimi; Tsuzaki, Kenji; Nishimura, Kenryo; Kiyonaga, Kenichi; Matsumoto, Yoko; Ueoka, Ryuichi

2006-05-01

416

EXTERIOR VIEW, THE SA WETSIDE BUILDING (ALSO KNOWN AS DISTILLATION ...  

Library of Congress Historic Buildings Survey, Historic Engineering Record, Historic Landscapes Survey

EXTERIOR VIEW, THE SA WETSIDE BUILDING (ALSO KNOWN AS DISTILLATION BUILDING OR SOLVAY TOWERS BUILDING) THE HEART OF THE SOLVAY PROCESS. VIEW LOOKING EAST. THIS BUILDING WAS BUILT IN 1954 TO REPLACE A SIMILAR STRUCTURE BUILT CIRCA 1907. - Solvay Process Company, SA Wetside Building, Between Willis & Milton Avenue, Solvay, Onondaga County, NY

417

Experimental study of multiple steady states in homogeneous azeotropic distillation  

Microsoft Academic Search

Bekiaris et al. (1993) explained the existence of multiple steady states in homogeneous ternary azeotropic distillation, on the basis of the analysis of the case of infinite reflux and infinite column length (infinite number of trays). They showed that the predictions of multiple steady states for such infinite columns have relevant implications for columns of finite length operated at finite

T. E. Guettinger; Cornelius Dorn; Manfred Morari

1997-01-01

418

Membrane Distillation and Related Operations—A Review  

Microsoft Academic Search

Membrane contactors represent an emerging technology in which the membrane is used as a tool for inter phase mass transfer operations: the membrane does not act as a selective barrier, but the separation is based on the phase equilibrium. In principle, all traditional stripping, scrubbing, absorption, evaporation, distillation, crystallization, emulsification, liquid?liquid extraction, and mass transfer catalysis processes can be carried

Efrem Curcio; Enrico Drioli

2005-01-01

419

VIEW LOOKING EAST, SA WETSIDE (DISTILLATION BUILDING) ON THE RIGHT, ...  

Library of Congress Historic Buildings Survey, Historic Engineering Record, Historic Landscapes Survey

VIEW LOOKING EAST, SA WETSIDE (DISTILLATION BUILDING) ON THE RIGHT, STD (SODA TOWER DRYERS?), SA DRYSIDE ON RIGHT. BEHIND STD BUILDING IS SHD BUILDING (SODA HORIZONTAL DRYERS?) THE ENTIRE DRYING COMPLEX WAS KNOWN AS THE DRYSIDE. - Solvay Process Company, SA Wetside Building, Between Willis & Milton Avenue, Solvay, Onondaga County, NY

420

Vacuum energy as dark matter  

NASA Astrophysics Data System (ADS)

We consider the vacuum energy of massive quantum fields in an expanding universe. We define a conserved renormalized energy-momentum tensor by means of a comoving cutoff regularization. Using exact solutions for de Sitter space-time, we show that in a certain range of mass and renormalization scales there is a contribution to the vacuum energy density that scales as nonrelativistic matter and that such a contribution becomes dominant at late times. By means of the WKB approximation, we find that these results can be extended to arbitrary Robertson-Walker geometries. We study the range of parameters in which the vacuum energy density would be compatible with current limits on dark matter abundance. Finally, by calculating the vacuum energy in a perturbed Robertson-Walker background, we obtain the speed of sound of density perturbations and show that the vacuum energy density contrast can grow on sub-Hubble scales as in standard cold dark matter scenarios.

Albareti, F. D.; Cembranos, J. A. R.; Maroto, A. L.

2014-12-01

421

Miniature Distillation Column for Producing LOX From Air  

NASA Technical Reports Server (NTRS)

The figure shows components of a distillation column intended for use as part of a system that produces high-purity liquid oxygen (LOX) from air by distillation. (The column could be easily modified to produce high-purity liquid nitrogen.) Whereas typical industrial distillation columns for producing high-purity liquid oxygen and/or nitrogen are hundreds of feet tall, this distillation column is less than 3 ft (less than about 0.9 m) tall. This column was developed to trickle-charge a LOX-based emergency oxygen system (EOS) for a large commercial aircraft. A description of the industrial production of liquid oxygen and liquid nitrogen by distillation is prerequisite to a meaningful description of the present miniaturized distillation column. Typically, such industrial production takes place in a chemical processing plant in which large quantities of high-pressure air are expanded in a turboexpander to (1) recover a portion of the electrical power required to compress the air and (2) partially liquefy the air. The resulting two-phase flow of air is sent to the middle of a distillation column. The liquid phase is oxygen-rich, and its oxygen purity increases as it flows down the column. The vapor phase is nitrogen-rich and its nitrogen purity increases as it flows up the column. A heater or heat exchanger, commonly denoted a reboiler, is at the bottom of the column. The reboiler is so named because its role is to reboil some of the liquid oxygen collected at the bottom of the column to provide a flow of oxygen-rich vapor. As the oxygen-rich vapor flows up the column, it absorbs the nitrogen in the down-flowing liquid by mass transfer. Once the vapor leaves the lower portion of the column, it interacts with down-flowing nitrogen liquid that has been condensed in a heat exchanger, commonly denoted a condenser, at the top of the column. Liquid oxygen and liquid nitrogen products are obtained by draining some of the purified product at the bottom and top of the column, respectively. Because distillation is a mass-transfer process, the purity of the product(s) can be increased by increasing the effectiveness of the mass-transfer process (increasing the mass-transfer coefficient) and/or by increasing the available surface area for mass transfer through increased column height. The diameter of a distillation column is fixed by pressure-drop and mass-flow requirements. The approach taken in designing the present distillation column to be short yet capable of yielding a product of acceptably high purity was to pay careful attention to design details that affect mass-transfer processes.

Rozzi, Jay C.

2006-01-01

422

Multi-saline sample distillation apparatus for hydrogen isotope analyses: Design and accuracy  

Microsoft Academic Search

A distillation apparatus for saline water samples was designed and tested. Six samples may be distilled simultaneously. The temperature was maintained at 400 C to ensure complete dehydration of the precipitating salts. Consequently, the error in the measured ratio of stable hydrogen isotopes resulting from incomplete dehydration of hydrated salts during distillation was eliminated.

A. A. Hassan

1981-01-01

423

27 CFR 28.192 - Packages of distilled spirits to be gauged.  

Code of Federal Regulations, 2010 CFR

...2010-04-01 false Packages of distilled spirits to be gauged. 28.192 Section 28...OF ALCOHOL Exportation of Distilled Spirits With Benefit of Drawback Filing of Notice...Removal § 28.192 Packages of distilled spirits to be gauged. Except for...

2010-04-01

424

Application of the self-heat recuperation technology to crude oil distillation  

Microsoft Academic Search

Crude oil distillation is an atmospheric distillation column using a furnace. It consumes about 50% of the energy required in an oil refinery plant. To reduce energy requirements, it is necessary to investigate crude oil distillation and to retrofit it with energy saving processes. Recently, the authors developed an innovative process design technology, termed self-heat recuperation technology for saving energy.

Yasuki Kansha; Akira Kishimoto; Atsushi Tsutsumi

425

Development of an Exploration-Class Cascade Distillation Subsystem: Performance Testing of the Generation 1.0 Prototype  

NASA Technical Reports Server (NTRS)

The ability to recover and purify water is crucial for realizing long-term human space missions. The National Aeronautics and Space Admininstration and Honeywell co-developed a five-stage vacuum rotary distillation water recovery system referred to as the Cascade Distillation Subsystem (CDS). Over the past three years, NASA's Advanced Exploration Systems (AES) Water Recovery Project (WRP) has been working toward the development of a flight-forward CDS design. In 2012 the original CDS prototype underwent a series of incremental upgrades and tests intened to both demonstrate the feasibility of a on-orbit demonstration of the system and to collect operational and performance data to be used to inform a second generation design. The latest testing of the CDS Generation 1.0 prototype was conducted May 29 through July 2, 2014. Initial system performance was benchmarked by processing deionized water and sodium chloride. Following, the system was challenged with analogue urine waste stream solutions stabilized with an Oxone-based and the two International Space Station baseline and alternative pretreatment solutions. During testing, the system processed more than 160 kilograms of wastewater with targeted water recoveries between 75 and 85% depending on the specific waste stream tested. For all wastewater streams, contaminant removals from wastewater feed to product water distillate, were estimated at greater than 99%. The average specific energy of the system was less than 120 Watt-hours/kilogram. The following paper provides detailed information and data on the performance of the CDS as challenged per the WRP test objectives.

Callahan, Michael R.; Sargusingh, Miriam J.

2015-01-01

426

Vacuum phenomenon: Clinical relevance.  

PubMed

Vacuum phenomenon (VP) is an anatomical entity of potential confusion in the diagnosis and evaluation of joint pathology. Observation of this phenomenon has been demonstrated on basic radiographs, computed tomography, and magnetic resonance imaging. Although VP is most often associated with degenerative joint disease, it is observed with other pathologies. Two problematic scenarios can occur: a false-positive diagnosis of serious pathology instead of benign VP and a false-negative diagnosis of benign VP with a more serious underlying process Despite this potential for confusion, criteria for distinguishing VP from other causes of joint pain and for evaluating a suspected case of VP have not been fully established. We reviewed the literature to determine underlying mechanism, symptomology, associated pathologies, and clinical importance of VP. The formation of VP can be explained by gas solubility, pressure-volume relationships, and human physiology. CT, GRE-MRI, and multipositional views are the best imaging studies to view VP. Although most cases of VP are benign, it can be associated with clinical signs and symptoms. VP outside the spine is an underreported finding on imaging studies. VP should be on the differential diagnosis for joint pain, especially in the elderly. We have proposed criteria for diagnosing VP and generated a basic algorithm for its workup. Underreporting of this phenomenon shows a lack of awareness of VP on the part of physicians. By identifying true anatomic VP, we can prevent harm from suboptimal treatment of patients. PMID:24288359

Gohil, Ishan; Vilensky, Joel A; Weber, Edward C

2014-04-01

427

Compact vacuum insulation  

DOEpatents

Improved compact insulation panel is provided which is comprised of two adjacent metal sheets spaced close together with a plurality of spherical, or other discretely shaped, glass or ceramic beads optimally positioned between the sheets to provide support and maintain the spacing between the metal sheets when the gases there between are evacuated to form a vacuum. These spherical glass beads provide the maximum support while minimizing thermal conductance. In its preferred embodiment; these two metal sheets are textured with ribs or concave protrusions in conjunction with the glass beads to maximize the structural integrity of the panels while increasing the spacing between beads, thereby reducing the number of beads and the number of thermal conduction paths. Glass or porcelain-enameled liners in combination with the glass spacers and metal sidewalls effectively decrease thermal conductivity, and various laminates, including wood, porcelain-enameled metal, and others effectively increase the strength and insulation capabilities of the panels. Also, a metal web is provided to hold the spacers in place, and strategic grooves are shown to accommodate expansion and contraction or shaping of the panels. 35 figs.

Benson, D.K.; Potter, T.F.

1992-10-27

428

Compact vacuum insulation  

DOEpatents

Improved compact insulation panel is provided which is comprised of two adjacent metal sheets spaced close together with a plurality of spherical, or other discretely shaped, glass or ceramic beads optimally positioned between the sheets to provide support and maintain the spacing between the metal sheets when the gases therebetween are evacuated to form a vacuum. These spherical glass beads provide the maximum support while minimizing thermal conductance. In its preferred embodiment; these two metal sheets are textured with ribs or concave protrusions in conjunction with the glass beads to maximize the structural integrity of the panels while increasing the spacing between beads, thereby reducing the number of beads and the number of thermal conduction paths. Glass or porcelain-enameled liners in combination with the glass spacers and metal sidewalls effectively decrease thermal conductivity, and variious laminates, including wood, porcelain-enameled metal, and others effectively increase the strength and insulation capabilities of the panels. Also, a metal web is provided to hold the spacers in place, and strategic grooves are shown to accommodate expansion and contraction or shaping of the panels.

Benson, David K. (Golden, CO); Potter, Thomas F. (Denver, CO)

1992-01-01

429

Vacuum plasma spray coating  

NASA Technical Reports Server (NTRS)

Currently, protective plasma spray coatings are applied to space shuttle main engine turbine blades of high-performance nickel alloys by an air plasma spray process. Originally, a ceramic coating of yttria-stabilized zirconia (ZrO2.12Y2O3) was applied for thermal protection, but was removed because of severe spalling. In vacuum plasma spray coating, plasma coatings of nickel-chromium-aluminum-yttrium (NiCrAlY) are applied in a reduced atmosphere of argon/helium. These enhanced coatings showed no spalling after 40 MSFC burner rig thermal shock cycles between 927 C (1700 F) and -253 C (-423 F), while current coatings spalled during 5 to 25 test cycles. Subsequently, a process was developed for applying a durable thermal barrier coating of ZrO2.8Y2O3 to the turbine blades of first-stage high-pressure fuel turbopumps utilizing the enhanced NiCrAlY bond-coating process. NiCrAlY bond coating is applied first, with ZrO2.8Y2O3 added sequentially in increasing amounts until a thermal barrier coating is obtained. The enchanced thermal barrier coating has successfully passed 40 burner rig thermal shock cycles.

Holmes, Richard R.; Mckechnie, Timothy N.

1989-01-01

430

Precooler Ring Vacuum System  

SciTech Connect

The precooler vacuum system, as proposed by FNAL, is based on a suitable modification of the existing Electron Cooling Ring System. Because of the magnetic cycle of the bending magnets, distributed ion pumping, as exists in the Electron Cooling Ring, is not applicable. Instead, the proposed pumping will be done with commercial appendage ion pumps mounted approximately every two meters around the circumference of the ring. The loss of effective pumping speed and non-uniformity of system pressure with appendage pumps may not be major considerations but the large number required does effect experimental and analytical equipment placement considerations. There is a distributed pumping technique available which: (1) is not affected by the magnetic cycle of the bending magnets; (2) will provide a minimum of four times the hydrogen pumping speed of the proposed appendage ion pumps; (3) will require no power during pumping after the strip is activated; (4) will provide the heat source for bakeout; (5) is easily replaceable; and (6) can be purchased, installed, and operated at a generous economic advantage over the presently proposed ion pumped system. The pumping technique referred to is non-evaporable gettering with ST101 Zr/Al pumping strip. A technical description of this pumping strip is given on Data Sheet 1 and 2 attached to this report.

Moenich, J.

1980-10-02

431

NCSX Vacuum Vessel Fabrication  

SciTech Connect

The National Compact Stellarator Experiment (NCSX) is being constructed at the Princeton Plasma Physics Laboratory (PPPL) in conjunction with the Oak Ridge National Laboratory (ORNL). The goal of this experiment is to develop a device which has the steady state properties of a traditional stellarator along with the high performance characteristics of a tokamak. A key element of this device is its highly shaped Inconel 625 vacuum vessel. This paper describes the manufacturing of the vessel. The vessel is being fabricated by Major Tool and Machine, Inc. (MTM) in three identical 120º vessel segments, corresponding to the three NCSX field periods, in order to accommodate assembly of the device. The port extensions are welded on, leak checked, cut off within 1" of the vessel surface at MTM and then reattached at PPPL, to accommodate assembly of the close-fitting modular coils that surround the vessel. The 120º vessel segments are formed by welding two 60º segments together. Each 60º segment is fabricated by welding ten press-formed panels together over a collapsible welding fixture which is needed to precisely position the panels. The vessel is joined at assembly by welding via custom machined 8" (20.3 cm) wide spacer "spool pieces." The vessel must have a total leak rate less than 5 X 10-6 t-l/s, magnetic permeability less than 1.02?, and its contours must be within 0.188" (4.76 mm). It is scheduled for completion in January 2006.

Viola, M. E.; Brown, T.; Heitzenroeder, P.; Malinowski, F.; Reiersen, W.; Sutton, L.; Goranson, P.; Nelson, B.; Cole, M.; Manuel, M.; McCorkle, D.

2005-10-07

432

Treatment of thoracic wounds with adapted vacuum therapy.  

PubMed

This is a report of seven cases of infected thoracic wounds treated with an adapted low-cost vacuum therapy in the Thoracic Surgery Unit of Santa Marcelina Hospital. The vacuum system used was designed and adapted to our hospital due to financial limitations on the acquisition of commercial kits. The vacuum-assisted closure kit used in this study consisted of chlorhexidine sponges (which are usually used for antisepsis of the surgical team), a 16F nasogastric tube, and two sterile adhesive films (OPSITE) for surgical field reinforcement. The mean duration of vacuum therapy was 13.4 days (range, 10-20 days), with an average of three dressing changes (range, 1-5). After treatment with vacuum-assisted closure, three wounds (3/7) were closed with simple primary sutures, one of the lesions (1/7) was closed by muscle flap rotation, and three wounds (3/7) healed by second intention. This adapted vacuum therapy was safe and easy to apply in our institution, including its use in patients with thoracostomies. PMID:24026077

de Abreu, Igor Renato L B; Pontes, Edgard P O; Tamagno, Mauro F L; Sardenberg, Rodrigo Afonso; Younes, Riad Naim; Abrão, Fernando Conrado

2014-01-01

433

Vacuum system of the cyclotrons in VECC, Kolkata  

SciTech Connect

The vacuum system of the K=130 Room Temperature Cyclotron (RTC) (operational since 1978) has been recently modernized and the same of the K{sub bend}=520 Superconducting Cyclotron (SCC), currently under commissioning, is being deployed for remote monitoring and control. The vacuum system of RTC is designed to achieve and maintain vacuum level of 2 X 10{sup -6} mbar inside 23 m{sup 3} volume of Resonator tank and DEE tank. This has been upgraded by replacing several valves, Freon units, gauges and pumps. The relay based manual control system has been replaced by PLC based automated system. The SCC vacuum system also has an elaborate arrangement comprising of turbo molecular pumping modules with associated isolation valves and characteristic gauges. This paper describes essential elements, typically used to obtain high (1X10{sup -7} mbar) vacuum using rotary pumps, diffusion pumps and cold traps/turbo-molecular pumps and other system components such as valves, gauges and baffles. The supervisory control methodology/scheme of both the vacuum systems, developed in-house using EPICS (Experimental Physics and Industrial Control System), a standard open-source software tool for designing distributed control system, is also elaborated here. (author)

Roy, Anindya; Bhole, R.B.; Akhtar, J.; Yadav, R.C.; Pal, Sarbajit; Sarkar, D.; Bhandari, R.K., E-mail: r_ani@vecc.gov.in, E-mail: rbb@vecc.gov.in, E-mail: javed@vecc.gov.in, E-mail: yadav@vecc.gov.in, E-mail: sarbajit@vecc.gov.in, E-mail: dsarkar@vecc.gov.in, E-mail: bhandari@vecc.gov.in [Variable Energy Cyclotron Centre, Kolkata (India)

2011-07-01

434

Vacuum energy and cosmological evolution  

E-print Network

An expanding universe is not expected to have a static vacuum energy density. The so-called cosmological constant $\\Lambda$ should be an approximation, certainly a good one for a fraction of a Hubble time, but it is most likely a temporary description of a true dynamical vacuum energy variable that is evolving from the inflationary epoch to the present day. We can compare the evolving vacuum energy with a Casimir device where the parallel plates slowly move apart ("expand"). The total vacuum energy density cannot be measured, only the effect associated to the presence of the plates, and then also their increasing separation with time. In the universe there is a nonvanishing spacetime curvature $R$ as compared to Minkowskian spacetime that is changing with the expansion. The vacuum energy density must change accordingly, and we naturally expect $\\delta\\Lambda\\sim R\\sim H^2$. A class of dynamical vacuum models that trace such rate of change can be constructed. They are compatible with the current cosmological data, and conveniently extended can account for the complete cosmic evolution from the inflationary epoch till the present days. These models are very close to the $\\Lambda$CDM model for the late universe, but very different from it at the early times. Traces of the inherent vacuum dynamics could be detectable in our recent past.

Joan Sola

2014-02-27

435

Vacuum Brazing of Accelerator Components  

NASA Astrophysics Data System (ADS)

Commonly used materials for accelerator components are those which are vacuum compatible and thermally conductive. Stainless steel, aluminum and copper are common among them. Stainless steel is a poor heat conductor and not very common in use where good thermal conductivity is required. Aluminum and copper and their alloys meet the above requirements and are frequently used for the above purpose. The accelerator components made of aluminum and its alloys using welding process have become a common practice now a days. It is mandatory to use copper and its other grades in RF devices required for accelerators. Beam line and Front End components of the accelerators are fabricated from stainless steel and OFHC copper. Fabrication of components made of copper using welding process is very difficult and in most of the cases it is impossible. Fabrication and joining in such cases is possible using brazing process especially under vacuum and inert gas atmosphere. Several accelerator components have been vacuum brazed for Indus projects at Raja Ramanna Centre for Advanced Technology (RRCAT), Indore using vacuum brazing facility available at RRCAT, Indore. This paper presents details regarding development of the above mentioned high value and strategic components/assemblies. It will include basics required for vacuum brazing, details of vacuum brazing facility, joint design, fixturing of the jobs, selection of filler alloys, optimization of brazing parameters so as to obtain high quality brazed joints, brief description of vacuum brazed accelerator components etc.

Singh, Rajvir; Pant, K. K.; Lal, Shankar; Yadav, D. P.; Garg, S. R.; Raghuvanshi, V. K.; Mundra, G.

2012-11-01

436

Preliminary obervations on use of ethanol distiller's by-products for polyculture of freshwater prawn (Macrobrachium rosenbergii) and golden shiner (Notemigonus crysoleucas)  

SciTech Connect

Two major by-products of ethanol distillation, corn distiller's solubles and corn distiller's mash, were evaluated for their potential use as a food source for freshwater prawn (Macrobrachium rosenbergii) and golden shiner (Notemigonus crysoleucas) in mid-western United States. Corn distiller's solubles were not found to be highly toxic to aquatic organisms at concentrations ranging up to 10,000 ppM. However, the high biological oxygen demand of the material requires that single applications not exceed 2000 ppM. Yield trials were conducted over a four month period in five 0.1 ha earthen ponds, located in proximity to an ethanol distillery. Each pond was stocked with 2000 postlarval shrimp (0.02 g mean weight). Three of these ponds were also each stocked with 75 adult golden shiner (27.0 g mean weight). One application of corn distiller's solubles (equivalent to approx. 2000 ppM) and three applications of corn distiller's mash (approx. 5 kg/application) were made over the course of the yield trails (approx. 120 days). No other food or fertilizer was added to the ponds. Survival of shrimp ranged from 34 to 75%. Survival of brood fish exceeded 90%. Mean weight of shrimp at harvest was approximately 12 g, and average production was equivalent to approximately 104 kg ha/sup -1/. Golden shiner reared in the same ponds as shrimp had production rates equivalent to approxmately 130 kg ha/sup -1/. The presence of fish did not appear to impede shrimp production. Although production results of fish and shrimp were encouraging, several factors existed which impeded production; these included: (1) little by-product was applied to ponds because the distillery was undergoing its shakedown period; (2) ponds were new and had minimal natural productivity; (3) grass was not fully established on the watershed and ponds became turbid; and (4) lower than normal temperatures prevailed over much of the growing period. 11 references, 2 figures, 8 tables.

Kohler, C.C.; Lewis, W.M.; Krueger, S.P.

1983-01-01

437

Graphoanalytical study on the economic effect of incorporating hydrocracking of the distillate feedstock in oil refineries of the fuel profile  

Microsoft Academic Search

1.To determine the possible range of application of the hydrocracking process in the oil refining industry, we have worked out a graphical method which makes it possible to determine a plant scheme incorporating catalytic cracking or hydrocracking units for the treatment of vacuum gas-oil and warranting a given total yield of light products and a given ratio between the yields

L. I. Erkina; Yu. I. Chernyi

1972-01-01

438

Vacuum Packaging of MEMS With Multiple Internal Seal Rings  

NASA Technical Reports Server (NTRS)

A proposed method of design and fabrication of vacuum-packaged microelectromechanical systems (MEMS) and of individual microelectromechanical devices involves the use of multiple internal seal rings (MISRs) in conjunction with vias (through holes plated with metal for electrical contacts). The proposed method is compatible with mass production in a wafer-level fabrication process, in which the dozens of MEMS or individual microelectromechanical devices on a typical wafer are simultaneously vacuum packaged by bonding a capping wafer before the devices are singulated (cut apart by use of a dicing saw). In addition to being compatible with mass production, the proposed method would eliminate the need for some complex and expensive production steps and would yield more reliable vacuum seals. Conventionally, each MEMS or individual microelectromechanical device is fabricated as one of many identical units on a device wafer. Vacuum packaging is accomplished by bonding the device wafer to a capping wafer with metal seal rings (one ring surrounding each unit) that have been formed on the capping wafer. The electrical leads of each unit are laid out on what would otherwise be a flat surface of the device wafer, against which the seal ring is to be pressed for sealing. The resulting pattern of metal lines and their insulating oxide coverings presents a very rough and uneven surface, upon which it is difficult to pattern the sealing metal. Consequently, the seal is prone to leakage unless additional costly and complex planarization steps are performed before patterning the seal ring and bonding the wafers.

Hayworth, Ken; Yee, Karl; Shcheglov, Kirill; Bae, Youngsam; Wiberg, Dean; Peay, Chris; Challoner, Anthony

2008-01-01

439

Contamination analysis unit  

DOEpatents

The portable Contamination Analysis Unit (CAU) measures trace quantifies of surface contamination in real time. The detector head of the portable contamination analysis unit has an opening with an O-ring seal, one or more vacuum valves and a small mass spectrometer. With the valve closed, the mass spectrometer is evacuated with one or more pumps. The O-ring seal is placed against a surface to be tested and the vacuum valve is opened. Data is collected from the mass spectrometer and a portable computer provides contamination analysis. The CAU can be used to decontaminate and decommission hazardous and radioactive surface by measuring residual hazardous surface contamination, such as tritium and trace organics It provides surface contamination data for research and development applications as well as real-time process control feedback for industrial cleaning operations and can be used to determine the readiness of a surface to accept bonding or coatings.

Gregg, Hugh R. (Livermore, CA); Meltzer, Michael P. (Livermore, CA)

1996-01-01

440

Contamination analysis unit  

DOEpatents

The portable Contamination Analysis Unit (CAU) measures trace quantities of surface contamination in real time. The detector head of the portable contamination analysis unit has an opening with an O-ring seal, one or more vacuum valves and a small mass spectrometer. With the valve closed, the mass spectrometer is evacuated with one or more pumps. The O-ring seal is placed against a surface to be tested and the vacuum valve is opened. Data is collected from the mass spectrometer and a portable computer provides contamination analysis. The CAU can be used to decontaminate and decommission hazardous and radioactive surfaces by measuring residual hazardous surface contamination, such as tritium and trace organics. It provides surface contamination data for research and development applications as well as real-time process control feedback for industrial cleaning operations and can be used to determine the readiness of a surface to accept bonding or coatings. 1 fig.

Gregg, H.R.; Meltzer, M.P.

1996-05-28

441

Einstein-?tsuki vacuum equations  

NASA Astrophysics Data System (ADS)

The generalisation of the Einstein vacuum theory to ?tsuki geometry is considered. It is shown that the theory based on Lagrangian density ?-gR is consistent and leads to a theory that is classically indistinguishable from the Einstein theory.

Smrz, P. K.

1993-01-01

442

Inhomogeneous and Interacting Vacuum Energy  

NASA Astrophysics Data System (ADS)

Vacuum energy is a simple model for dark energy driving an accelerated expansion of the universe. If the vacuum energy is inhomogeneous in spacetime then it must be interacting. We present the general equations for a spacetime-dependent vacuum energy in cosmology, including inhomogeneous perturbations. We show how any dark energy cosmology can be described by an interacting vacuum+matter. Different models for the interaction can lead to different behaviour (e.g., sound speed for dark energy perturbations) and hence could be distinguished by cosmological observations. As an example we present the cosmic microwave microwave background anisotropies and the matter power spectrum for two different versions of a generalised Chaplygin gas cosmology.

De-Santiago, Josue; Wands, David; Wang, Yuting

443

Vacuum lamination of photovoltaic modules  

NASA Technical Reports Server (NTRS)

Vacuum lamination of terrestrial photovoltaic modules is a new high volume process requiring new equipment and newly develop materials. Equipment development, materials research, and some research in related fields and testing methods are discussed.

Burger, D. R.

1982-01-01

444

Vacuum system pump down analysis  

SciTech Connect

My assignment on the SP-100 Vacuum Vessel Vacuum System Team was to perform a transient pump down analysis for the vacuum vessel that will house the SP-100 reactor during testing. Pump down time was calculated for air and helium. For all cases the proposed vacuum system will be able to pump down the vessel within the required time. The use of a larger rotary piston pump (DUO250) improves the pump down time by 35 minutes and therefore should be considered. The 6-inch duct for the roughing line is optimal, however, because all cases are well below the 24 hour time frame, the 4-inch duct is sufficient. The use of the single turbomolecular pump during pump down is sufficient. A pump down with helium in the vessel and a helium inleakage delays the time to achieve the base pressure marginally and is acceptable.

Rohrdanz, D.R.

1990-08-01

445

Very-Low-Cost, Rugged Vacuum System  

NASA Technical Reports Server (NTRS)

NASA, DoD, DHS, and commercial industry have a need for miniaturized, rugged, low-cost vacuum systems. Recent advances in sensor technology have led to the development of very small mass spectrometer detectors as well as other miniature analytical instruments. However, the vacuum systems to support these sensors remain large, heavy, and power-hungry. To meet this need, a miniaturized vacuum system was created based on a very small, rugged, and inexpensive- to-manufacture molecular drag pump (MDP). The MDP is enabled by the development of a miniature, veryhigh- speed, rugged, low-power, brushless DC motor optimized for wide temperature operation and long life. Such a pump represents an order-of-magnitude reduction in mass, volume, and cost over current, commercially available, state-ofthe- art vacuum pumps. The vacuum system consists of the MDP coupled to a ruggedized rough pump (for terrestrial applications or for planets with substantial atmospheres). The rotor in the MDP consists of a simple smooth cylinder of aluminum spinning at approximately 200,000 RPM inside an outer stator housing. The pump stator comprises a cylindrical aluminum housing with one or more specially designed grooves that serve as flow channels. To minimize the length of the pump, the gas is forced down the flow channels of the outer stator to the base of the pump. The gas is then turned and pulled toward the top through a second set of channels cut into an inner stator housing that surrounds the motor. The compressed gas then flows down channels in the motor housing to the exhaust port of the pump. The exhaust port of the pump is connected to a diaphragm or scroll pump. This pump delivers very high performance in a very small envelope. The design was simplified so that a smaller compression ratio, easier manufacturing process, and enhanced ruggedness can be achieved at the lowest possible cost. The machining of the rotor and stators is very simple compared to that necessary to fabricate TMP (turbo molecular pump) rotor and stator blades. Also, the symmetry of the rotor is such that dynamic balancing of the rotor is greatly simplified. Finally, because of the simplified design, the number of parts in the unit is cut by nearly a factor of three. In fact, there are only five parts, not counting the motor and off-the-shelf screws and O-rings. This reduces the amount of machining and also makes fit-up much simpler while allowing the maintenance of close tolerances.

Kline-Schoder, Robert; Sorensen, Paul; Passow, Christian; Bilski, Steve

2013-01-01

446

Vacuum Variable Medium Temperature Blackbody  

Microsoft Academic Search

This article describes the vacuum variable medium-temperature blackbody (VMTBB) constructed to serve as a highly stable reference\\u000a source with an aperture diameter of 20 mm in the temperature range from 150 °C to 430 °C under medium-vacuum conditions (10?3 Pa) and in a reduced background environment (liquid-nitrogen-cooled shroud). The VMTBB was realized for the calibration facility\\u000a at the PTB in the field of

S. P. Morozova; N. A. Parfentiev; B. E. Lisiansky; U. A. Melenevsky; B. Gutschwager; C. Monte; J. Hollandt

2010-01-01

447

Distillation of nonstabilizer states for universal quantum computation  

NASA Astrophysics Data System (ADS)

Magic-state distillation is a fundamental technique for realizing fault-tolerant universal quantum computing and produces high-fidelity Clifford eigenstates, called magic states, which can be used to implement the non-Clifford ?/8 gate. We propose an efficient protocol for distilling other nonstabilizer states that requires only Clifford operations, measurement, and magic states. One critical application of our protocol is efficiently and fault-tolerantly implementing arbitrary, non-Clifford, single-qubit rotations in, on average, constant online circuit depth and polylogarithmic (in precision) offline resource cost, resulting in significant improvements over state-of-the-art decomposition techniques. Finally, we show that our protocol is robust to noise in the resource states.

Duclos-Cianci, Guillaume; Svore, Krysta M.

2013-10-01

448

A cryogenic distillation column for the XENON1T experiment  

NASA Astrophysics Data System (ADS)

The XENON collaboration aims for the direct detection of cold dark matter in form of weakly interacting massive particles (WIMPs). A dual phase time projection chamber filled with liquid xenon is used to detect the WIMP-nucleon interaction. For the next generation experiment XENON1T with an active target mass of 1 ton of xenon, a new distillation column to remove krypton out of xenon to a concentration of < 5 × 10?13 (0.5 ppt) natural krypton in xenon is designed and tested at the Institut für Kernphysik, Universitat Munster. The experimental setup together with two diagnostic tools is presented, as well as one stability test of a 11 hour distillation run at the designed flowrate of 3 kg per hour.

Rosendahl, S.; Brown, E.; Cristescu, I.; Fieguth, A.; Huhmann, C.; Murra, M.; Weinheimer, C.

2014-11-01

449

Rearing of sea lamprey, Petromyzon marinus, embryos in distilled water  

USGS Publications Warehouse

Most embryological studies of lampreys in the Great Lakes have been conducted with filtered water from Lake Huron. Although this water was entirely satisfactory for the earlier work, the present need for knowledge of the effects of various compounds on embryological development requires that the initial medium be sterile. The purpose of the present study was to determine whether sea lamprey embryos could be successfully reared in distilled water. Mature sea lampreys were collected from the Ocqueoc River, Presque Isle County, Michigan, and transferred to the Hammond Bay Biological Station where eggs were stripped and fertilized according to the method of Piavis. After activation was ascertained to be 90-100% complete, the embryos were washed 3-5 timesexperimentals with commercially obtained U.S.P. distilled water and controls with filtered Lake Huron water.

Piavis, George W.; Howell, John H.

1969-01-01

450

Distillation and purification of symmetric entangled Gaussian states  

SciTech Connect

We propose an entanglement distillation and purification scheme for symmetric two-mode entangled Gaussian states that allows to asymptotically extract a pure entangled Gaussian state from any input entangled symmetric Gaussian state. The proposed scheme is a modified and extended version of the entanglement distillation protocol originally developed by Browne et al. [Phys. Rev. A 67, 062320 (2003)]. A key feature of the present protocol is that it utilizes a two-copy degaussification procedure that involves a Mach-Zehnder interferometer with single-mode non-Gaussian filters inserted in its two arms. The required non-Gaussian filtering operations can be implemented by coherently combining two sequences of single-photon addition and subtraction operations.

Fiurasek, Jaromir [Department of Optics, Palacky University, 17. listopadu 12, CZ-77146 Olomouc (Czech Republic)

2010-10-15

451

Thin layer distillation for matrix isolation in flow analysis.  

PubMed

Analyte transfer from the matrix in a thin layer distillation (TLD) cell and its subsequent measurement were investigated in a flow injection configuration. We designed the cell such that the donor and acceptor streams flowed in parallel channels separated by a thin dividing wall. The matrix transfer process involved room-temperature distillation of the analyte into the headspace of the TLD cell and its subsequent condensation/uptake by a concurrently flowing acceptor stream. There are no membranes; hence there are no membrane-related problems. The TLD system design was optimized with respect to its dimensions and operational parameters. Throughput and sensitivity were compared with a conventional pervaporation flow injection (PFI) system for ammonia and five different amines. For the higher molecular mass amines, the TLD approach provided comparable or superior performance. The TLD technique should be an attractive approach for online analysis of volatile chemical species in 'dirty' samples, especially for volatile analytes of higher molecular mass. PMID:19071680

Mornane, Patrick; van den Haak, Jeroen; Cardwell, Terence J; Cattrall, Robert W; Dasgupta, Purnendu K; Kolev, Spas D

2007-04-30

452

Vacuum Refining of Molten Silicon  

NASA Astrophysics Data System (ADS)

Metallurgical fundamentals for vacuum refining of molten silicon and the behavior of different impurities in this process are studied. A novel mass transfer model for the removal of volatile impurities from silicon in vacuum induction refining is developed. The boundary conditions for vacuum refining system—the equilibrium partial pressures of the dissolved elements and their actual partial pressures under vacuum—are determined through thermodynamic and kinetic approaches. It is indicated that the vacuum removal kinetics of the impurities is different, and it is controlled by one, two, or all the three subsequent reaction mechanisms—mass transfer in a melt boundary layer, chemical evaporation on the melt surface, and mass transfer in the gas phase. Vacuum refining experimental results of this study and literature data are used to study the model validation. The model provides reliable results and shows correlation with the experimental data for many volatile elements. Kinetics of phosphorus removal, which is an important impurity in the production of solar grade silicon, is properly predicted by the model, and it is observed that phosphorus elimination from silicon is significantly increased with increasing process temperature.

Safarian, Jafar; Tangstad, Merete

2012-12-01

453

Reactive Distillation for Esterification of Bio-based Organic Acids  

SciTech Connect

The following is the final report of the three year research program to convert organic acids to their ethyl esters using reactive distillation. This report details the complete technical activities of research completed at Michigan State University for the period of October 1, 2003 to September 30, 2006, covering both reactive distillation research and development and the underlying thermodynamic and kinetic data required for successful and rigorous design of reactive distillation esterification processes. Specifically, this project has led to the development of economical, technically viable processes for ethyl lactate, triethyl citrate and diethyl succinate production, and on a larger scale has added to the overall body of knowledge on applying fermentation based organic acids as platform chemicals in the emerging biorefinery. Organic acid esters constitute an attractive class of biorenewable chemicals that are made from corn or other renewable biomass carbohydrate feedstocks and replace analogous petroleum-based compounds, thus lessening U.S. dependence on foreign petroleum and enhancing overall biorefinery viability through production of value-added chemicals in parallel with biofuels production. Further, many of these ester products are candidates for fuel (particularly biodiesel) components, and thus will serve dual roles as both industrial chemicals and fuel enhancers in the emerging bioeconomy. The technical report from MSU is organized around the ethyl esters of four important biorenewables-based acids: lactic acid, citric acid, succinic acid, and propionic acid. Literature background on esterification and reactive distillation has been provided in Section One. Work on lactic acid is covered in Sections Two through Five, citric acid esterification in Sections Six and Seven, succinic acid in Section Eight, and propionic acid in Section Nine. Section Ten covers modeling of ester and organic acid vapor pressure properties using the SPEAD (Step Potential Equilibrium and Dynamics) method.

Fields, Nathan; Miller, Dennis J.; Asthana, Navinchandra S.; Kolah, Aspi K.; Vu, Dung; Lira, Carl T.

2008-09-23

454

Determination of phenols using simultaneous steam distillation-extraction.  

PubMed

Simultaneous distillation-extraction was proposed as a preconcentration step for the determination of phenol and its derivatives in aqueous and soil samples. Detection limits of 0.01 mg l(-1) (water) and 0.1 mg kg(-1) (soil) were achieved by gas chromatography-flame ionization detection. The described preconcentration procedure was applied for the primary study of the adsorption equilibrium in a water-soil system serving as a model of phenol behaviors in the environment. PMID:10670728

Barták, P; Frnková, P; Cáp, L

2000-01-21

455

Refiner\\/marketer targets production of transportation fuels and distillates  

Microsoft Academic Search

Citgo Petroleum Corp., the wholly owned subsidiary of Petroleos de Venezuela, S.A. (PDVSA), the Venezuelan national oil company, owns two gasoline producing refineries, a 305,000-b\\/d system in Lake Charles, La., and a 130,000-b\\/d facility in Corpus Christi, Texas. Each is considered a deep conversion facility capable of converting heavy, sour crudes into a high percentage of transportation fuels and distillates.

Thompson

1997-01-01

456

Effects of System Densities on Distillation Column Performance  

Microsoft Academic Search

Distillation experiments were carried out on three binary systems (ethanol—butanol, ethanol—propan-2-ol, and propan-2-ol-butanol) in a 0.1-m internal diameter glass column packed with 8 mm diameter Raschig rings. The experiments were performed under total reflux conditions and at atmospheric pressure. The data collected on column performance showed that performance declined with increasing average bulk liquid density. The results also lend credence

S. O. Fasesan; S. A. Sanni; E. A. Taiwo

1998-01-01

457

Synthesis and design of optimal thermal membrane distillation networks  

E-print Network

) Madhav Nyapathi Seshu , B.E., R.V. College of Engineering, Bangalore, India Chair of Advisory Committee: Dr. Mahmoud El-Halwagi Thermal membrane distillation is one of the novel separation methods in the process industry. It involves the simultaneous... regions of the parametric space. Two case studies have been presented to illustrate the applicability of the presented methodology. iv ACKNOWLEDGMENTS I would like to express my gratitude to Dr. Mahmoud El-Halwagi for his guidance and support...

Nyapathi Seshu, Madhav

2006-10-30

458

Distillation of secret key and entanglement from quantum states  

Microsoft Academic Search

We study and solve the problem of distilling a secret key from quantum states representing correlation between two parties (Alice and Bob) and an eavesdropper (Eve) via one-way public discussion: we prove a coding theorem to achieve the 'wire-tapper' bound, the difference of the mutual information Alice-Bob and that of Alice-Eve, for so-called classical-quantum-quantum-correlations, via one-way public communication. This result

Igor Devetak; Andreas Winter

2005-01-01

459

Distillation of hydrogen isotopes for polarized HD target  

Microsoft Academic Search

We have developed a cryogenic distillation system to purify Hydrogen-Deuteride (HD) gas for a polarized HD target in LEPS experiments at SPring-8. A small amount of ortho-H$_2$ ($\\\\sim$0.01%) in the HD gas plays an important role in efficiently polarizing the HD target. Since there are 1$\\\\sim$5% impurities of H$_2$ and D$_2$ in commercially available HD gases, it is inevitable that

T. Ohta; S. Bouchigny; J.-P. Didelez; M. Fujiwara; K. Fukuda; H. Kohri; T. Kunimatsu; C. Morisaki; S. Ono; G. Rouill; M. Tanaka; K. Ueda; M. Uraki; M. Utsuro; S. Y. Wang; M. Yosoi

2011-01-01

460

Distillation of hydrogen isotopes for polarized HD targets  

Microsoft Academic Search

We have developed a new cryogenic distillation system to purify Hydrogen-Deuteride (HD) gas for polarized HD targets in LEPS experiments at SPring-8. A small amount of ortho-H2 (?0.01%) in the HD gas plays an important role in efficiently polarizing the HD target. Since there are 1–5% impurities of H2 and D2 in commercially available HD gases, it is necessary to

T. Ohta; S. Bouchigny; J.-P. Didelez; M. Fujiwara; K. Fukuda; H. Kohri; T. Kunimatsu; C. Morisaki; S. Ono; G. Rouillé; M. Tanaka; K. Ueda; M. Uraki; M. Utsuro; S. Y. Wang; M. Yosoi

461

Distillation of hydrogen isotopes for polarized HD target  

E-print Network

We have developed a cryogenic distillation system to purify Hydrogen-Deuteride (HD) gas for a polarized HD target in LEPS experiments at SPring-8. A small amount of ortho-H$_2$ ($\\sim$0.01%) in the HD gas plays an important role in efficiently polarizing the HD target. Since there are 1$\\sim$5% impurities of H$_2$ and D$_2$ in commercially available HD gases, it is inevitable that the HD gas is purified up to $\\sim$99.99%. The distillation system has a cryogenic pot (17$\\sim$21 K) containing many small stainless steel cells called Heli-pack. Commercial HD gas with an amount of 5.2 mol is fed into the pot. We carried out three distillation runs by changing temperatures (17.5 K and 20.5 K) and gas extraction speeds (1.3 ml/min and 5.2 ml/min). The extracted gas was analyzed by using a gas analyzer system combining a quadrupole mass spectrometer with a gas chromatograph. The HD gas of 1 mol with a purity better than 99.99% has been successfully obtained. The effective NTS (Number of Theoretical Stages), which is an indicator of the distillator performances, is obtained as 37.2$\\pm$0.6. This value is in reasonable agreement with a designed value of 37.9. The HD target is expected to be efficiently polarized under a well-controlled condition by doping an optimal amount of ortho-H$_2$ to the purified HD gas.

T. Ohta; S. Bouchigny; J. -P. Didelez; M. Fujiwara; K. Fukuda; H. Kohri; T. Kunimatsu; C. Morisaki; S. Ono; G. Rouill'; M. Tanaka; K. Ueda; M. Uraki; M. Utsuro; S. Y. Wang; M. Yosoi

2011-12-12

462

Analysis of Closed Multivessel Batch Distillation of Ternary Azeotropic Mixtures  

E-print Network

. An indirect level control strategy is implemented that eliminates the need for pre-calculated vessel holdups- posed a closed (total reflux) operation of the conventional batch distillation column with a condenser Condenser D Middle 3 2 1 2 1 x + 12B xF 1N N N D x x x x M xM B N Figure 1: Steadystate compositionprofile

Skogestad, Sigurd

463

Corrosion control program maximizes crude-unit reliability  

SciTech Connect

A corrosion control program was started at Texaco Refining and Marketing Inc.'s Wilmington, Calif., refinery in 1985 to determine corrosion problem areas in the distillation facilities, and to establish effective corrosion control procedures to improve the reliability of the distillation unit. A total control program approach was used. Corrosion mechanisms and variables affecting corrosion were first identified, and then recommendations for mechanical and operating modifications were given. The primary subject matter of the article is divided into the following areas: Crude slate; Overhead system; Crude-unit experience; Light ends fractionation; Corrosion mechanisms; Crude dewatering benefits; Chloride reduction; Amine application; Inhibitor feed optimization; Acid/base balance.

Powell, J.T.; Rue, J.R.; Mansouri, M.M.

1989-03-20

464

Volatile organic emissions from the distillation and pyrolysis of vegetation  

NASA Astrophysics Data System (ADS)

Leaf and woody plant tissue (Pinus ponderosa, Eucalyptus saligna, Quercus gambelli, Saccharum officinarum and Oriza sativa) were heated from 30 to 300°C and volatile organic compound (VOC) emissions were identified and quantified. Major VOC emissions were acetic acid, furylaldehyde, methyl acetate, pyrazine, terpenes, 2,3-butadione, phenol and methanol, as well as smaller emissions of furan, acetone, acetaldehyde, acetonitrile and benzaldehyde. Total VOC emissions from distillation and pyrolysis were on the order of 10 mgC/gC dry weight of vegetation, as much as 33% and 44% of CO2 emissions (gC(VOC)/gC(CO2)) measured during the same experiments, in air and nitrogen atmospheres, respectively. The emissions are similar in identity and quantity to those from smoldering combustion of woody tissue and of different character than those evolved during flaming combustion. VOC emissions from the distillation of pools and the pyrolysis of vegetation heated under low turbulence conditions produces concentrations near leaves that reach the lower limits of flammability and the emissions may be important in the propagation of wildfires. VOC emissions from charcoal production are also related to distillation and pyrolysis; the emissions of the highly reactive VOCs from production are as large as the carbon monoxide emissions.

Greenberg, J. P.; Friedli, H.; Guenther, A. B.; Hanson, D.; Harley, P.; Karl, T.

2005-09-01

465

Volatile organic emissions from the distillation and pyrolysis of vegetation  

NASA Astrophysics Data System (ADS)

Leaf and woody plant tissue (Pinus ponderosa, Eucalyptus saligna, Quercus gambelli, Saccharum officinarum and Oriza sativa) were heated from 30 to 300°C and volatile organic compound (VOC) emissions were identified and quantified. Major VOC emissions were mostly oxygenated and included acetic acid, furylaldehyde, acetol, pyrazine, terpenes, 2,3-butadione, phenol and methanol, as well as smaller emissions of furan, acetone, acetaldehyde, acetonitrile and benzaldehyde. Total VOC emissions from distillation and pyrolysis were on the order of 10 gC/kgC dry weight of vegetation, as much as 33% and 44% of CO2 emissions (gC(VOC)/gC(CO2)) measured during the same experiments, in air and nitrogen atmospheres, respectively.

The emissions are similar in identity and quantity to those from smoldering combustion of woody tissue and of different character than those evolved during flaming combustion. VOC emissions from the distillation of pools and endothermic pyrolysis under low turbulence conditions may produce flammable concentrations near leaves and may facilitate the propagation of wildfires. VOC emissions from charcoal production are also related to distillation and pyrolysis; the emissions of the highly reactive VOCs from production are as large as the carbon monoxide emissions.

Greenberg, J. P.; Friedli, H.; Guenther, A. B.; Hanson, D.; Harley, P.; Karl, T.

2006-01-01

466

Distillation of hydrogen isotopes for polarized HD target  

E-print Network

We have developed a cryogenic distillation system to purify Hydrogen-Deuteride (HD) gas for a polarized HD target in LEPS experiments at SPring-8. A small amount of ortho-H$_2$ ($\\sim$0.01%) in the HD gas plays an important role in efficiently polarizing the HD target. Since there are 1$\\sim$5% impurities of H$_2$ and D$_2$ in commercially available HD gases, it is inevitable that the HD gas is purified up to $\\sim$99.99%. The distillation system has a cryogenic pot (17$\\sim$21 K) containing many small stainless steel cells called Heli-pack. Commercial HD gas with an amount of 5.2 mol is fed into the pot. We carried out three distillation runs by changing temperatures (17.5 K and 20.5 K) and gas extraction speeds (1.3 ml/min and 5.2 ml/min). The extracted gas was analyzed by using a gas analyzer system combining a quadrupole mass spectrometer with a gas chromatograph. The HD gas of 1 mol with a purity better than 99.99% has been successfully obtained. The effective NTS (Number of Theoretical Stages), which is...

Ohta, T; Didelez, J -P; Fujiwara, M; Fukuda, K; Kohri, H; Kunimatsu, T; Morisaki, C; Ono, S; Rouill', G; Tanaka, M; Ueda, K; Uraki, M; Utsuro, M; Wang, S Y; Yosoi, M

2011-01-01

467

IN VITRO STUDIES ON THE EFFECT OF SCREENING PROCESSED CORN DISTILLERS SOLUBLES AND CENTRIFUGE PROCESSED CORN DISTILLERS SOLUBLES ON CELLULOSE DIGESTION AND MICROBIAL PROTEIN SYNTHESIS 1 ,2  

Microsoft Academic Search

SUMMARY A series of in vitro fermentation trials were conducted to investigate the effect of screening processed distillers solubles (SDS) and centri- fuge processed distillers solubles (CDS) on cel- lulose digestion, microbial protein synthesis and forage dry matter digestion. The possible dif- ference between SDS and CDS was also sur- veyed by adding 1 ml each of valeric acid (10

M. C. Chen; W. M. Beeson; T. W. Perry

2010-01-01

468

Production of Si by vacuum carbothermal reduction of SiO2 using concentrated solar energy  

NASA Astrophysics Data System (ADS)

Using concentrated solar radiation as the energy source of high-temperature process heat, the carbothermal reduction of silica to silicon was examined thermodynamically and demonstrated experimentally at vacuum pressures. Reducing the system pressure favors Si(g) formation, enabling its vacuum distillation. Experimentation in a solar reactor was performed in the range 1,997-2,263 K at ˜3×10-3 bar with mixtures of charcoal and silica directly exposed to radiative flux intensities equivalent to 6,500 suns, yielding Si purities ranging from 66.1-79.2 wt.%. The Si purity increased with temperature. Solid characterizations showed SiC and SiO as important reaction intermediaries.

Loutzenhiser, Peter G.; Tuerk, Ozan; Steinfeld, Aldo

2010-09-01

469

Measurement of partial pressures in vacuum technology and vacuum physics  

NASA Technical Reports Server (NTRS)

It is pointed out that the measurement of gaseous pressures of less than 0.0001 torr is based on the ionization of gas atoms and molecules due to collisions with electrons. The particle density is determined in place of the pressure. The ionization cross sections for molecules of various gases are discussed. It is found that the true pressure in a vacuum system cannot be determined with certainty if it is unknown which gas is present. Effects of partial pressure determination on the condition of the vacuum system are discussed together with ion sources, systems of separation, and ion detection.

Huber, W. K.

1986-01-01

470

Vacuum as a hyperbolic metamaterial  

E-print Network

As demonstrated by Chernodub, vacuum in a strong magnetic field behaves as a periodic Abrikosov vortex lattice in a type-II superconductor. We investigate electromagnetic behavior of vacuum in this state. Since superconductivity is realized along the axis of magnetic field only, strong anisotropy of the vacuum dielectric tensor is observed. The diagonal components of the tensor are positive in the x and y directions perpendicular to the magnetic field, and negative in the z direction along the field. As a result, vacuum behaves as a hyperbolic metamaterial medium. If the magnetic field is constant, low frequency extraordinary photons experience this medium as a (3+1) Minkowski spacetime in which the role of time is played by the spatial z coordinate. Spatial variations of the magnetic field curve this effective spacetime, and may lead to formation of "event horizons", which are analogous to electromagnetic black holes in hyperbolic metamaterials. We also note that hyperbolic metamaterials behave as diffractionless "perfect lenses". Since large enough magnetic fields probably had arisen in the course of evolution of early Universe, the demonstrated hyperbolic behavior of early vacuum may have imprints in the large scale structure of the present-day Universe.

Igor I. Smolyaninov

2011-08-10

471

The Light-Front Vacuum  

E-print Network

Background: The vacuum in the light-front representation of quantum field theory is trivial while vacuum in the equivalent canonical representation of the same theory is non-trivial. Purpose: Understand the relation between the vacuum in light-front and canonical representations of quantum field theory and the role of zero-modes in this relation. Method: Vacuua are defined as linear functionals on an algebra of field operators. The role of the algebra in the definition of the vacuum is exploited to understand this relation. Results: The vacuum functional can be extended from the light-front Fock algebra to an algebra of local observables. The extension to the algebra of local observables is responsible for the inequivalence. The extension defines a unitary mapping between the physical representation of the local algebra and a sub-algebra of the light-front Fock algebra. Conclusion: There is a unitary mapping from the physical representation of the algebra of local observables to a sub-algebra of the light-fro...

Herrmann, Marc

2015-01-01

472

Effects of acid extrusion on the degradability of maize distillers dried grain with solubles in pigs.  

PubMed

Commonly used feed processing technologies are not sufficient to affect recalcitrant nonstarch polysaccharides (NSP) such as arabinoxylans present in maize distillers dried grain with solubles (DDGS). Instead, hydrothermal treatments combined with acid catalysts might be more effective to modify these NSP. The objective of this experiment was to investigate the effects of hydrothermal maleic acid treatment (acid extrusion) on the degradability of maize DDGS in growing pigs. It was hypothesized that acid extrusion modifies DDGS cell wall architecture and thereby increases fermentability of NSP. Two diets, containing either 40% (wt/wt) unprocessed or acid-extruded DDGS, were restrictedly fed to groups of gilts (n=11, with 4 pigs per group; initial mean BW: 20.8±0.2 kg) for 18 d and performance and digestibility were analyzed. Acid extrusion tended to decrease apparent ileal digestibility (AID) of CP (approximately 3 percentage units [% units]); P=0.063) and starch (approximately 1% unit; P=0.096). Apparent digestibility of CP and starch measured at the mid colon (2% units, P=0.030, for CP and 0.3% units, P<0.01, for starch) and apparent total tract digestibility (ATTD; 3% units, P<0.01, for CP and 0.2% units, P=0.024, for starch) were lower for the acid-extruded diet compared with the control diet. Hindgut disappearance was, however, not different between diets, indicating that reduced CP and starch digestibility were mainly due to decreased AID. Acid extrusion tended to increase AID of NSP (6% units; P=0.092) and increased digestibility of NSP measured at the mid colon (6% units; P<0.01), whereas hindgut disappearance and ATTD of NSP did not differ between diets. Greater NSP digestibility was mainly due to greater digestibility of arabinosyl, xylosyl, and glucosyl residues, indicating that both arabinoxylan and cellulose degradability were affected by acid extrusion. In conclusion, these results show that acid extrusion did not improve degradation of DDGS for growing pigs. Although acid extrusion seemed to facilitate more rapid degradation of NSP and shifted fermentation to more proximal gastrointestinal segments, total extent of NSP degradation was not affected. More than 35% of the NSP from DDGS remained undegraded, independent of technological processing. Enzyme technologies that specifically target ester-linked acetyl, feroloyl, or coumaroyl groups were identified to be of interest for future research. PMID:25367528

de Vries, S; Pustjens, A M; van Rooijen, C; Kabel, M A; Hendriks, W H; Gerrits, W J J

2014-12-01

473

RF cavity vacuum interlock system  

NASA Astrophysics Data System (ADS)

The Continuous Electron Beam Accelerator Facility (CEBAF), a continuous wave (CW) 4 GeV Electron Accelerator is undergoing construction in Newport News, Virginia. When completed in 1994, the accelerator will be the largest installation of radio-frequency superconductivity. Production of cryomodules, the fundamental building block of the machine, has started. A cryomodule consists of four sets of pairs of 1497 MHz, 5 cell niobium cavities contained in separate helium vessels and mounted in a cryostat with appropriate end caps for helium supply and return. Beam vacuum of the cavities, the connecting beam piping, the waveguides, and the cryostat insulating vacuum are crucial to the performance of the machine. The design and initial experience of the vacuum systems for the first 2 1/4 cryomodules that makeup the 45 MEV injector are discussed.

Jordan, K.; Crawford, K.; Bundy, R.; Dylla, H. F.; Heckman, J.; Marshall, J.; Nichols, R.; Osullivan, S.; Preble, J.; Robb, J.

1992-03-01

474

D-Zero Vacuum System  

SciTech Connect

The system pumping speed was calculated by taking the reciprocal of the sum of the reciprocal pump speed and the reciprocal line conductances. The conductances of the pipe were calculated from the following formulas taken from the Varian vacuum manual. This report updates the original to reflect the pumping curves and basic vacuum system characteristics for the purchased components and installed piping of the D-Zero vacuum system. The system consists of two Edward's E2M275 two stage mechanical pumps, a Leybold-Heraeus WSU2000 Blower and three Varian 4' diffusion pumps (one for each cryostat). Individual pump and system pumping speed curves and a diagram of the system is included.

Wintercorn, S.J.; /Fermilab

1986-04-07

475

Isokinetic vs still air sampling of asbestos fiber emission from high-velocity, low-volume vacuum systems  

E-print Network

flow was shown graphically and was used in the analysis of each vacuum. In order to correct for vacuum cleaner filter loading, continuous velocity measurements were taken through-out each test with a thermoanemometer. The two sampling methods gave... Minerals 5 I I. Suction Pressure Measurements III. Data from the Still Air Study IV. Statistical Unit Arrangement V. Analysis of Variance Table for the Two-Way Classification 19 31 32 33 VI VII VII I IX Pitot Traverse Measurements of Vacuum...

Grabowski, John S

1979-01-01

476

Vacuum Plasma Spraying Replaces Electrodeposition  

NASA Technical Reports Server (NTRS)

Vacuum plasma spraying used to fabricate large parts with complicated contours and inner structures, without uninspectable welds. Reduces time, and expense of fabrication. Wall of combustion chamber built up inside of outer nickel-alloy jacket by plasma spraying. Particles of metal sprayed partially melted in plasma gun and thrown at supersonic speed toward deposition surface. Vacuum plasma-spray produces stronger bond between the grooves and covering layer completing channels and wall of combustion chamber. In tests, bond withstood pressure of 20 kpsi, three times allowable limit by old method.

Holmes, Richard R.; Power, Chris; Burns, David H.; Daniel, Ron; Mckechnie, Timothy N.

1992-01-01

477

Compactification, Vacuum Energy and Quintessence  

E-print Network

We study the possibility that the vacuum energy density of scalar and internal-space gauge fields arising from the process of dimensional reduction of higher dimensional gravity theories plays the role of quintessence. We show that, for the multidimensional Einstein-Yang-Mills system compactified on a $R \\times S^3 \\times S^d$ topology, there are classically stable solutions such that the observed accelerated expansion of the Universe at present can be accounted for without upsetting structure formation scenarios or violating observational bounds on the vacuum energy density.

M. C. Bento; O. Bertolami

1999-05-20

478

Relativistic invariance of the vacuum  

NASA Astrophysics Data System (ADS)

Relativistic invariance of the vacuum is (or follows from) one of the Wightman axioms, which is commonly believed to be true. Without these axioms, here we present a direct and general proof of continuous relativistic invariance of all real-time vacuum correlations of fields, not only scattering (forward in time), based on closed time path formalism. The only assumptions are basic principles of relativistic quantum field theories: the relativistic invariance of the Lagrangian, of the form including known interactions (electromagnetic, weak and strong), and standard rules of quantization. The proof is in principle perturbative leaving a possibility of spontaneous violation of invariance. Time symmetry is, however, manifestly violated.

Bednorz, Adam

2013-12-01

479

Method for vacuum fusion bonding  

DOEpatents

An improved vacuum fusion bonding structure and process for aligned bonding of large area glass plates, patterned with microchannels and access holes and slots, for elevated glass fusion temperatures. Vacuum pumpout of all components is through the bottom platform which yields an untouched, defect free top surface which greatly improves optical access through this smooth surface. Also, a completely non-adherent interlayer, such as graphite, with alignment and location features is located between the main steel platform and the glass plate pair, which makes large improvements in quality, yield, and ease of use, and enables aligned bonding of very large glass structures.

Ackler, Harold D. (Sunnyvale, CA); Swierkowski, Stefan P. (Livermore, CA); Tarte, Lisa A. (Livermore, CA); Hicks, Randall K. (Stockton, CA)

2001-01-01

480

QED vacuum loops and Inflation  

E-print Network

A QED-based model of a new version of Vacuum Energy has recently been suggested, which leads to a simple, finite, one parameter representation of Dark Energy. An elementary, obvious, but perhaps radical generalization is then able to describe both Dark Energy and Inflation in the same framework of Vacuum Energy. One further, obvious generalization then leads to a relation between Inflation and the Big Bang, to the automatic inclusion of Dark Matter, and to a possible understanding of the birth (and death) of a Universe.

H. M. Fried; Y. Gabellini

2014-11-19

481

Distillation time effect on lavender essential oil yield and composition.  

PubMed

Lavender (Lavandula angustifolia Mill.) is one of the most widely grown essential oil crops in the world. Commercial extraction of lavender oil is done using steam distillation. The objective of this study was to evaluate the effect of the length of the distillation time (DT) on lavender essential oil yield and composition when extracted from dried flowers. Therefore, the following distillation times (DT) were tested in this experiment: 1.5 min, 3 min, 3.75 min, 7.5 min, 15 min, 30 min, 60 min, 90 min, 120 min, 150 min, 180 min, and 240 min. The essential oil yield (range 0.5-6.8%) reached a maximum at 60 min DT. The concentrations of cineole (range 6.4-35%) and fenchol (range 1.7-2.9%) were highest at the 1.5 min DT and decreased with increasing length of the DT. The concentration of camphor (range 6.6-9.2%) reached a maximum at 7.5-15 min DT, while the concentration of linalool acetate (range 15-38%) reached a maximum at 30 min DT. Results suggest that lavender essential oil yield may not increase after 60 min DT. The change in essential oil yield, and the concentrations of cineole, fenchol and linalool acetate as DT changes were modeled very well by the asymptotic nonlinear regression model. DT may be used to modify the chemical profile of lavender oil and to obtain oils with differential chemical profiles from the same lavender flowers. DT must be taken into consideration when citing or comparing reports on lavender essential oil yield and composition. PMID:23535305

Zheljazkov, Valtcho D; Cantrell, Charles L; Astatkie, Tess; Jeliazkova, Ekaterina

2013-01-01

482

The Influence of Distillation Conditions on the Azeotropic Composition  

NASA Astrophysics Data System (ADS)

The thermodynamic conditions that determine the presence of an azeotrope in a binary solution are developed and analyzed together with the criteria that define if the azeotrope has a maximum or minimum boiling point at constant pressure. It is shown that using simple models for describing vapor-liquid equilibria and vapor pressure data of the pure components it is possible to determine rather accurately how the azeotropic point will shift if the distillation is carried out at a different pressure or temperature. Examples are given on the use of the proposed method; these can be used as classroom material.

Wisniak, Jaime

1998-11-01

483

Preliminary Design Program: Vapor Compression Distillation Flight Experiment Program  

NASA Technical Reports Server (NTRS)

This document provides a description of the results of a program to prepare a preliminary design of a flight experiment to demonstrate the function of a Vapor Compression Distillation (VCD) Wastewater Processor (WWP) in microgravity. This report describes the test sequence to be performed and the hardware, control/monitor instrumentation and software designs prepared to perform the defined tests. the purpose of the flight experiment is to significantly reduce the technical and programmatic risks associated with implementing a VCD-based WWP on board the International Space Station Alpha.

Schubert, F. H.; Boyda, R. B.

1995-01-01

484

Development of a preprototype vapor compression distillation water recovery subsystem  

NASA Technical Reports Server (NTRS)

The activities involved in the design, development, and test of a preprototype vapor compression distillation water recovery subsystem are described. This subsystem, part of a larger regenerative life support evaluation system, is designed to recover usable water from urine, urinal rinse water, and concentrated shower and laundry brine collected from three space vehicle crewmen for a period of 180 days without resupply. Details of preliminary design and testing as well as component developments are included. Trade studies, considerations leading to concept selections, problems encountered, and test data are also presented. The rework of existing hardware, subsystem development including computer programs, assembly verification, and comprehensive baseline test results are discussed.

Johnson, K. L.

1978-01-01

485

Pneumatically Actuated Miniature Peristaltic Vacuum Pumps  

NASA Technical Reports Server (NTRS)

Pneumatically actuated miniature peristaltic vacuum pumps have been proposed for incorporation into advanced miniature versions of scientific instruments that depend on vacuum for proper operation. These pumps are expected to be capable of reaching vacuum-side pressures in the torr to millitorr range (from .133 down to .0.13 Pa). Vacuum pumps that operate in this range are often denoted roughing pumps. In comparison with previously available roughing pumps, these pumps are expected to be an order of magnitude less massive and less power-hungry. In addition, they would be extremely robust, and would operate with little or no maintenance and without need for oil or other lubricants. Portable mass spectrometers are typical examples of instruments that could incorporate the proposed pumps. In addition, the proposed pumps could be used as roughing pumps in general laboratory applications in which low pumping rates could be tolerated. The proposed pumps could be designed and fabricated in conventionally machined and micromachined versions. A typical micromachined version (see figure) would include a rigid glass, metal, or plastic substrate and two layers of silicone rubber. The bottom silicone layer would contain shallow pump channels covered by silicone arches that could be pushed down pneumatically to block the channels. The bottom silicone layer would be covered with a thin layer of material with very low gas permeability, and would be bonded to the substrate everywhere except in the channel areas. The top silicone layer would be attached to the bottom silicone layer and would contain pneumatic- actuation channels that would lie crosswise to the pump channels. This version is said to be micromachined because the two silicone layers containing the channels would be fabricated by casting silicone rubber on micromachined silicon molds. The pneumatic-actuation channels would be alternately connected to a compressed gas and (depending on pump design) either to atmospheric pressure or to a partial vacuum source. The design would be such that the higher pneumatic pressure would be sufficient to push the silicone arches down onto the substrates, blocking the channels. Thus, by connecting pneumatic- actuation channels to the two pneumatic sources in spatial and temporal alternation, waves of opening and closing, equivalent to peristalsis, could be made to move along the pump channels. A pump according to this concept could be manufactured inexpensively. Pneumatic sources (compressors and partial vacuum sources) similar those needed for actuation are commercially available; they typically have masses of .100 g and power demands of the order of several W. In a design-optimization effort, it should be possible to reduce masses and power demands below even these low levels and to integrate pneumatic sources along with the proposed pumps into miniature units with overall dimensions of no more than a few centimeters per side.

Feldman, Sabrina; Feldman, Jason; Svehla, Danielle

2003-01-01

486

Experimental and analytical studies of hydrocarbon yields under dry-, steam-, and steam-with-propane distillation  

E-print Network

injection 3 1.1.2 Steam distillation……………………………… 4 1.2 Objectives of study………..………………………………. 7 1.2.1 Deliverables…………………………………… 8 1.2.2 Model applications…………………………….. 8 II LITERATURE REVIEW……………………………………….. 9 III STEAM DISTILLATION...…………………………………. 24 3.3 Analytical models…………………………………………. 30 IV EXPERIMENTAL APPARATUS AND PROCEDURE………. 33 4.1 Experimental apparatus…………………………………… 33 4.1.1 Fluid injection system…………………………. 35 4.1.2 Distillation cell………………………………... 35 viii CHAPTER...

Jaiswal, Namit

2007-09-17

487

Rhamnolipid produced by Pseudomonas aeruginosa USM-AR2 facilitates crude oil distillation.  

PubMed

A biosurfactant-producing and hydrocarbon-utilizing bacterium, Pseudomonas aeruginosa USM-AR2, was used to assist conventional distillation. Batch cultivation in a bioreactor gave a biomass of 9.4 g L(-1) and rhamnolipid concentration of 2.4 g L(-1) achieved after 72 h. Biosurfactant activity (rhamnolipid) was detected by the orcinol assay, emulsification index and drop collapse test. Pretreatment of crude oil TK-1 and AG-2 with a culture of P. aeruginosa USM-AR2 that contains rhamnolipid was proven to facilitate the distillation process by reducing the duration without reducing the quality of petroleum distillate. It showed a potential in reducing the duration of the distillation process, with at least 2- to 3-fold decreases in distillation time. This is supported by GC-MS analysis of the distillate where there was no difference between compounds detected in distillate obtained from treated or untreated crude oil. Calorimetric tests showed the calorie value of the distillate remained the same with or without treatment. These two factors confirmed that the quality of the distillate was not compromised and the incubation process by the microbial culture did not over-degrade the oil. The rhamnolipid produced by this culture was the main factor that enhanced the distillation performance, which is related to the emulsification of hydrocarbon chains in the crude oil. This biotreatment may play an important role to improve the existing conventional refinery and distillation process. Reducing the distillation times by pretreating the crude oil with a natural biosynthetic product translates to energy and cost savings in producing petroleum products. PMID:22688247

Asshifa Md Noh, Nur; Al-Ashraf Abdullah, Amirul; Nasir Mohamad Ibrahim, Mohamad; Ramli Mohd Yahya, Ahmad

2012-01-01

488

Vacuum Fizeau wedge wavemeter for pulsed uv lasers  

SciTech Connect

We have constructed and tested a vacuum-spaced Fizeau wedge wavemeter that is suitable for measuring the wavelength of pulsed or continuous-wave lasers over the range of 630 nm to 200 nm. A Lasertechnics Model 100 Fizeau wavemeter was modified for ultraviolet operation and demonstrated an accuracy of 1.6 parts in 10/sup 5/ at 248 nm. Extensive computer modeling of the wavemeter has provided optimized design parameters for an improved unit. 9 refs., 6 figs., 2 tabs.

Reiser, C.; Lykke, K.R.

1988-08-01

489

Demetallization, detarring and desulfurization of distillation residues. [Comparison of available technologies  

Microsoft Academic Search

At the present stage of technical development, only catalytic pressure hydrogenation appears feasible for desulfurizing distillation residues. New detarring and demetallization processes are also reviewed.

Riediger

1976-01-01

490

Reactive Distillation and Air Stripping Processes for Water Recycling and Trace Contaminant Control  

NASA Technical Reports Server (NTRS)

Reactive distillation designs are considered to reduce the presence of volatile organic compounds in the purified water. Reactive distillation integrates a reactor with a distillation column. A review of the literature in this field has revealed a variety of functional reactive columns in industry. Wastewater may be purified by a combination of a reactor and a distiller (e.g., the EWRS or VPCAR concepts) or, in principle, through a design which integrates the reactor with the distiller. A review of the literature in reactive distillation has identified some different designs in such combinations of reactor and distiller. An evaluation of reactive distillation and reactive air stripping is presented with regards to the reduction of volatile organic compounds in the contaminated water and air. Among the methods presented, an architecture is presented for the evaluation of the simultaneous oxidation of organics in air and water. These and other designs are presented in light of potential improvements in power consumptions and air and water purities for architectures which include catalytic activity integrated into the water processor. In particular, catalytic oxidation of organics may be useful as a tool to remove contaminants that more traditional distillation and/or air stripping columns may not remove. A review of the current leading edge at the commercial level and at the research frontier in catalytically active materials is presented. Themes and directions from the engineering developments in catalyst design are presented conceptually in light of developments in the nanoscale chemistry of a variety of catalyst materials.

Boul, Peter J.; Lange, Kevin E.; Conger, Bruce; Anderson, Molly

2009-01-01

491

Vacuum barrier for excimer lasers  

DOEpatents

A barrier for separating the vacuum area of a diode from the pressurized gas area of an excimer laser. The barrier is a composite material comprising layers of a metal such as copper, along with layers of polyimide, and a matrix of graphite fiber yarns impregnated with epoxy. The barrier is stronger than conventional foil barriers, and allows greater electron throughput. 3 figs.

Shurter, R.P.

1992-09-15

492

Vacuum-insulated catalytic converter  

DOEpatents

A catalytic converter has an inner canister that contains catalyst-coated substrates and an outer canister that encloses an annular, variable vacuum insulation chamber surrounding the inner canister. An annular tank containing phase-change material for heat storage and release is positioned in the variable vacuum insulation chamber a distance spaced part from the inner canister. A reversible hydrogen getter in the variable vacuum insulation chamber, preferably on a surface of the heat storage tank, releases hydrogen into the variable vacuum insulation chamber to conduct heat when the phase-change material is hot and absorbs the hydrogen to limit heat transfer to radiation when the phase-change material is cool. A porous zeolite trap in the inner canister absorbs and retains hydrocarbons from the exhaust gases when the catalyst-coated substrates and zeolite trap are cold and releases the hydrocarbons for reaction on the catalyst-coated substrate when the zeolite trap and catalyst-coated substrate get hot.

Benson, David K. (Golden, CO)

2001-01-01

493

Plates for vacuum thermal fusion  

DOEpatents

A process for effectively bonding arbitrary size or shape substrates. The process incorporates vacuum pull down techniques to ensure uniform surface contact during the bonding process. The essence of the process for bonding substrates, such as glass, plastic, or alloys, etc., which have a moderate melting point with a gradual softening point curve, involves the application of an active vacuum source to evacuate interstices between the substrates while at the same time providing a positive force to hold the parts to be bonded in contact. This enables increasing the temperature of the bonding process to ensure that the softening point has been reached and small void areas are filled and come in contact with the opposing substrate. The process is most effective where at least one of the two plates or substrates contain channels or grooves that can be used to apply vacuum between the plates or substrates during the thermal bonding cycle. Also, it is beneficial to provide a vacuum groove or channel near the perimeter of the plates or substrates to ensure bonding of the perimeter of the plates or substrates and reduce the unbonded regions inside the interior region of the plates or substrates.

Davidson, James C. (Livermore, CA); Balch, Joseph W. (Livermore, CA)

2002-01-01

494

Quantum Vacuum Structure and Cosmology  

SciTech Connect

Contemporary physics faces three great riddles that lie at the intersection of quantum theory, particle physics and cosmology. They are: (1) The expansion of the universe is accelerating - an extra factor of two appears in the size; (2) Zero-point fluctuations do not gravitate - a matter of 120 orders of magnitude; and (3) The 'True' quantum vacuum state does not gravitate. The latter two are explicitly problems related to the interpretation and the physical role and relation of the quantum vacuum with and in general relativity. Their resolution may require a major advance in our formulation and understanding of a common unified approach to quantum physics and gravity. To achieve this goal we must develop an experimental basis and much of the discussion we present is devoted to this task. In the following, we examine the observations and the theory contributing to the current framework comprising these riddles. We consider an interpretation of the first riddle within the context of the universe's quantum vacuum state, and propose an experimental concept to probe the vacuum state of the universe.

Rafelski, Johann; Labun, Lance; Hadad, Yaron; /Arizona U. /Munich U.; Chen, Pisin; /Taiwan, Natl. Taiwan U. /KIPAC, Menlo Park /SLAC

2011-12-05

495

Cleaner Vacuum-Bag Curing  

NASA Technical Reports Server (NTRS)

Improvement upon recommended procedures saves time and expense. Autoclave molding in vacuum bag cleaner if adhesive-backed covering placed around caul plate as well as on mold plate. Covering easy to remove after curing and leaves caul plate free of resin deposits.

Clemons, J. M.; Penn, B. G.; Ledbetter, Frank E., III; Daniels, J. G.

1987-01-01

496

HIGH PRODUCTIVITY VACUUM BLASTING SYSTEM  

SciTech Connect

The purpose of the project is to increase the productivity and economics of existing vacuum blasting technology. This technology is used to remove radioactive contamination, PCB's and lead-base paint and provides worker and environmental protection by continuously recycling the blast media and the full containment of the dust generated in the process.

Dr. M.A. Ebadian

2000-01-13

497

Vacuum barrier for excimer lasers  

DOEpatents

A barrier for separating the vacuum area of a diode from the pressurized gas area of an excimer laser. The barrier is a composite material comprising layers of a metal such as copper, along with layers of polyimide, and a matrix of graphite fiber yarns impregnated with epoxy. The barrier is stronger than conventional foil barriers, and allows greater electron throughput.

Shurter, Roger P. (Jemez Springs, NM)

1992-01-01

498

Vacuum Seal Permits Limited Rotation  

NASA Technical Reports Server (NTRS)

Flexible metal seal permits rotation of object in vacuum chamber. Seal made from two cylindrical azimuthally fluted bellows attached to ends of cylindrical axially fluted bellows with connecting tubes at both ends. Designed for rotation of sample probes in electron spectroscopy for chemical analysis (ESCA), other applications likely.

Lombardi, F.

1985-01-01

499

Vacuum-injection-molding processing  

SciTech Connect

An improved processing technique for the manufacture of glass or glass-ceramic headers has been developed. Vacuum-injection molding is a relatively easy processing technique that has been used successfully in the fabrication of several different advantages in certain applications over the present fabrication process which uses glass preforms.

Kramer, D.P.; Massey, R.T.

1982-01-01

500

Vacuum mounting for piezoelectric transducers  

NASA Technical Reports Server (NTRS)

Special housing couples piezoelectric transducers to nonporous surfaces for ultrasonic or acoustic-emission testing. Device, while providing sound isolation on flat or nonflat surfaces, can be attached and detached quickly. Vacuum sealing mechanism eliminates need for permanent or semipermanent bonds, viscous coupling liquids, weights, magnets, tape, or springs ordinarily used.

Tiede, D. A.

1977-01-01