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|a (TOE)ost6885185
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|a (TOE)6885185
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|a TOE
|c TOE
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|a GDWR
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|a 09
|2 edbsc
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|a E 1.99:doe/r5/10240-01
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|a E 1.99:doe/r5/10240-01
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|a doe/r5/10240-01
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|a Ethanol production by vapor compression distillation
|h [electronic resource]
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|a Argonne, Ill. :
|b United States. Dept. of Energy. Chicago Operations Office ;
|a Oak Ridge, Tenn. :
|b distributed by the Office of Scientific and Technical Information, U.S. Dept. of Energy,
|c 1981.
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300 |
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|a Pages: 10 :
|b digital, PDF file.
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|a text
|b txt
|2 rdacontent.
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|a computer
|b c
|2 rdamedia.
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|a online resource
|b cr
|2 rdacarrier.
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|a Published through the Information Bridge: DOE Scientific and Technical Information.
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|a 01/01/1981.
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|a "doe/r5/10240-01"
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|a Ellis, G.S.
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|a Ellis (George S.), Chardon, OH (USA)
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|a The goal of this project is to develop and demonstrate a one gallon per hour vapor compression distillation unit for fuel ethanol production that can be profitably manufactured and economically operated by individual family units. Vapor compression distillation is already an industrially accepted process and this project's goal is to demonstrate that it can be done economically on a small scale. Theoretically, the process is independent of absolute pressure. It is only necessary that the condenser be at higher pressure than the evaporator. By reducing the entire process to a pressure of approximately 0.1 atmosphere, the evaporation and condensation can occur at near ambient temperature. Even though this approach requires a vacuum pump, and thus will not represent the final cost effective design, it does not require preheaters, high temperature materials, or as much insulation as if it were to operate a near ambient pressure. Therefore, the operation of the ambient temperature unit constitutes the first phase of this project. Presently, the ambient temperature unit is fully assembled and has begun testing. So far it has successfully separated ethanol from a nine to one diluted input solution. However the production rate has been very low.
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536 |
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|b FG02-80R510240.
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650 |
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|a Vapor Condensers.
|2 local.
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650 |
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7 |
|a Design.
|2 local.
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650 |
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7 |
|a Testing.
|2 local.
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650 |
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7 |
|a Distillation.
|2 local.
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650 |
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7 |
|a Ethanol.
|2 local.
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650 |
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7 |
|a Organic Compounds.
|2 local.
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7 |
|a Separation Processes.
|2 local.
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650 |
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7 |
|a Condensers.
|2 local.
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7 |
|a Distillation Equipment.
|2 local.
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7 |
|a Hydroxy Compounds.
|2 local.
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7 |
|a Equipment.
|2 local.
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7 |
|a Alcohols.
|2 local.
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|a Biomass Fuels.
|2 edbsc.
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1 |
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|a United States.
|b Department of Energy.
|b Chicago Operations Office.
|4 res.
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710 |
1 |
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|a United States.
|b Department of Energy.
|b Office of Scientific and Technical Information.
|4 dst.
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|u http://www.osti.gov/servlets/purl/6885185/
|z Online Access
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907 |
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|a .b73552161
|b 03-07-23
|c 04-24-13
|
998 |
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|a web
|b 04-24-13
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|i 1
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|p Can circulate
|a University of Colorado Boulder
|b Online
|c Online
|d Online
|e E 1.99:doe/r5/10240-01
|h Superintendent of Documents classification
|i web
|n 1
|