Biological production of fuels from coal-derived gases: Quarterly report, June 20, 1987-September 20, 1987
The technical feasibility of converting CO, H/sub 2/ and CO/sub 2/ from synthesis gas to ethanol and acetate has been demonstrated in a continuous stirred-tank reactor with both continuous gas and liquid feed. This report describes the equipment and procedures for continuous operation, as well as steady-state experiments carried out at three steady-state conditions. Although the operating conditions for continuous operation have not been optimized and a significant amount of acetate remains in the product stream, the feasibility of using a bacterial process for synthesis gas conversion to liquid fuels has been demonstrated. Future work during subsequent contracts should concentrate on producing a single liquid fuel as a product, increasing the product concentration, and defining and optimizing reaction conditions for maximizing, product yield. 3 refs., 17 figs.
- Research Organization:
- Arkansas Univ., Fayetteville (USA)
- DOE Contract Number:
- AC22-85PC80012
- OSTI ID:
- 5700172
- Report Number(s):
- DOE/PC/80012-T8; ON: DE88002518
- Resource Relation:
- Other Information: Portions of this document are illegible in microfiche products
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
59 BASIC BIOLOGICAL SCIENCES
BIOCONVERSION
CARBON DIOXIDE
CARBON MONOXIDE
HYDROGEN
SYNTHESIS GAS
ACETATES
BIOCHEMICAL REACTION KINETICS
BIOREACTORS
CELL CULTURES
CHEMICAL REACTORS
CONVERSION RATIO
ETHANOL
GAS FLOW
LIQUEFACTION
LIQUID FLOW
LIQUID FUELS
METHANE
MICROORGANISMS
PROGRESS REPORT
STEADY-STATE CONDITIONS
ALCOHOLS
ALKANES
CARBON COMPOUNDS
CARBON OXIDES
CARBOXYLIC ACID SALTS
CHALCOGENIDES
DOCUMENT TYPES
ELEMENTS
FLUID FLOW
FLUIDS
FUELS
GASES
HYDROCARBONS
HYDROXY COMPOUNDS
KINETICS
NONMETALS
ORGANIC COMPOUNDS
OXIDES
OXYGEN COMPOUNDS
REACTION KINETICS
THERMOCHEMICAL PROCESSES
010405* - Coal
Lignite
& Peat- Hydrogenation & Liquefaction
550500 - Metabolism