Production of oil from coal. [Methods, hydrogenation process, Fischer--Tropsch process, purification and composition adjustment, gasification economics, synthesis, temperature, pressure, H:CO ratio, catalysts, and synthesis economics]
Journal Article
·
· Coke Gas
OSTI ID:5306330
- OSTI ID:
- 5306330
- Journal Information:
- Coke Gas, Vol. 13
- Country of Publication:
- United States
- Language:
- English
Similar Records
Production of hydrocarbons by synthesis. [Effects of catalysts, temperature, and pressure on coal hydrogenation and Fischer-Tropsch process]
Production of liquid fuels from coal in Central Queensland. [Two methods presented are: Fischer--Tropsch synthesis and direct hydrogenation; comparison of Sasol and H-Coal processes; latter was considered to be more economical; hydrogenation of coal paste at 400 to 500/sup 0/C and 100 to 200 atm]
Coal gas as a substitute for synthesis gas in the Fischer--Tropsch synthesis. II. Effect of catalyst composition and temperature upon activity and product distribution. [Four different Ni catalysts at atmospheric pressure and 180, 190, and 200/sup 0/ for conversion effect on purified coal gas samples; catalysts were 100 Ni:10 MgO:5 ThO/sub 2/:100 kieselguhr (k), 100 Ni:10 Al/sub 2/O/sub 3/:100 k, 100 Ni:25 MnO:10 Al/sub 2/O/sub 3/:100 k, and 50 Ni:50 Co:10 MgO:5 ThO/sub 2/:200 k; reaction is mainly CO + 2H/sub 2/ = (CH/sub 2/:) + H/sub 2/O]
Journal Article
·
Sun Jan 01 00:00:00 EST 1939
· Petroleum Z.
·
OSTI ID:5306330
Production of liquid fuels from coal in Central Queensland. [Two methods presented are: Fischer--Tropsch synthesis and direct hydrogenation; comparison of Sasol and H-Coal processes; latter was considered to be more economical; hydrogenation of coal paste at 400 to 500/sup 0/C and 100 to 200 atm]
Journal Article
·
Mon Jan 01 00:00:00 EST 1968
· J. Inst. Eng., Aust.
·
OSTI ID:5306330
Coal gas as a substitute for synthesis gas in the Fischer--Tropsch synthesis. II. Effect of catalyst composition and temperature upon activity and product distribution. [Four different Ni catalysts at atmospheric pressure and 180, 190, and 200/sup 0/ for conversion effect on purified coal gas samples; catalysts were 100 Ni:10 MgO:5 ThO/sub 2/:100 kieselguhr (k), 100 Ni:10 Al/sub 2/O/sub 3/:100 k, 100 Ni:25 MnO:10 Al/sub 2/O/sub 3/:100 k, and 50 Ni:50 Co:10 MgO:5 ThO/sub 2/:200 k; reaction is mainly CO + 2H/sub 2/ = (CH/sub 2/:) + H/sub 2/O]
Journal Article
·
Thu Jan 01 00:00:00 EST 1959
· U. Technol., Bengal Eng. Coll.
·
OSTI ID:5306330
Related Subjects
01 COAL, LIGNITE, AND PEAT
FISCHER-TROPSCH SYNTHESIS
FUEL OILS
PRODUCTION
SYNTHETIC FUELS
CATALYSTS
COAL
ECONOMICS
CARBONACEOUS MATERIALS
CHEMICAL REACTIONS
ENERGY SOURCES
FOSSIL FUELS
FUELS
OILS
ORGANIC COMPOUNDS
OTHER ORGANIC COMPOUNDS
PETROLEUM PRODUCTS
010405* - Coal
Lignite
& Peat- Hydrogenation & Liquefaction
FISCHER-TROPSCH SYNTHESIS
FUEL OILS
PRODUCTION
SYNTHETIC FUELS
CATALYSTS
COAL
ECONOMICS
CARBONACEOUS MATERIALS
CHEMICAL REACTIONS
ENERGY SOURCES
FOSSIL FUELS
FUELS
OILS
ORGANIC COMPOUNDS
OTHER ORGANIC COMPOUNDS
PETROLEUM PRODUCTS
010405* - Coal
Lignite
& Peat- Hydrogenation & Liquefaction