Methanation for coal hydrogasification. [Substantial fraction of product gas is CO, CO/sub 2/, and H, which are catalytically converted to CH/sub 3/; Ni-on-alumina catalyst used]
Journal Article
·
· Am. Chem. Soc., Div. Gas Fuel Chem., Prepr.
OSTI ID:5184156
- Research Organization:
- Inst. Gas Technol., Chicago, Ill
- OSTI ID:
- 5184156
- Journal Information:
- Am. Chem. Soc., Div. Gas Fuel Chem., Prepr., Vol. 14:4 (Pt. 1)
- Country of Publication:
- United States
- Language:
- English
Similar Records
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]
Cleanup methanation for hydrogasification process. [Conversion of coal hydrogasification product gas to high Btu gas; catalytic activities of Ni, Fe, and Ru catalysts for methanation of CO measured; Ni on kieselguhr found to be most active]
Methane manufacture from carbon dioxide and hydrogen. [Gas of >15% CO/sub 2/ converted to CH/sub 4/ in 2 stages over Ni catalyst at 180-250/sup 0/ at atmospheric or elevated pressure; catalyst of 60% Ni, 30% kieselguhr, 10% MgO; CO/sub 2/--H conversion 84. 5% in 1st stage and 90% in 2nd or 98-9% total yield]
Journal Article
·
Thu Jan 01 00:00:00 EST 1959
· U. Technol., Bengal Eng. Coll.
·
OSTI ID:5184156
Cleanup methanation for hydrogasification process. [Conversion of coal hydrogasification product gas to high Btu gas; catalytic activities of Ni, Fe, and Ru catalysts for methanation of CO measured; Ni on kieselguhr found to be most active]
Journal Article
·
Sun Jan 01 00:00:00 EST 1967
· Adv. Chem. Ser.
·
OSTI ID:5184156
Methane manufacture from carbon dioxide and hydrogen. [Gas of >15% CO/sub 2/ converted to CH/sub 4/ in 2 stages over Ni catalyst at 180-250/sup 0/ at atmospheric or elevated pressure; catalyst of 60% Ni, 30% kieselguhr, 10% MgO; CO/sub 2/--H conversion 84. 5% in 1st stage and 90% in 2nd or 98-9% total yield]
Patent
·
Sat Nov 26 00:00:00 EST 1955
·
OSTI ID:5184156
Related Subjects
01 COAL, LIGNITE, AND PEAT
COAL
METHANATION
COAL GASIFICATION
HIGH BTU GAS
PRODUCTION
CHEMICAL REACTION KINETICS
METHANE
ALUMINIUM OXIDES
CATALYSTS
EQUIPMENT
NICKEL
ALKANES
ALUMINIUM COMPOUNDS
CARBONACEOUS MATERIALS
CHALCOGENIDES
CHEMICAL REACTIONS
CRYOGENIC FLUIDS
ELEMENTS
ENERGY SOURCES
FLUIDS
FOSSIL FUELS
FUEL GAS
FUELS
GASES
GASIFICATION
HYDROCARBONS
KINETICS
METALS
ORGANIC COMPOUNDS
OXIDES
OXYGEN COMPOUNDS
REACTION KINETICS
TRANSITION ELEMENTS
010404* - Coal
Lignite
& Peat- Gasification
COAL
METHANATION
COAL GASIFICATION
HIGH BTU GAS
PRODUCTION
CHEMICAL REACTION KINETICS
METHANE
ALUMINIUM OXIDES
CATALYSTS
EQUIPMENT
NICKEL
ALKANES
ALUMINIUM COMPOUNDS
CARBONACEOUS MATERIALS
CHALCOGENIDES
CHEMICAL REACTIONS
CRYOGENIC FLUIDS
ELEMENTS
ENERGY SOURCES
FLUIDS
FOSSIL FUELS
FUEL GAS
FUELS
GASES
GASIFICATION
HYDROCARBONS
KINETICS
METALS
ORGANIC COMPOUNDS
OXIDES
OXYGEN COMPOUNDS
REACTION KINETICS
TRANSITION ELEMENTS
010404* - Coal
Lignite
& Peat- Gasification