Pipeline gas from coal by methanation of synthesis gas. [Over 90% H + CO conversion to methane maintained for extended periods operating at 30-300 psig and 600-900/sup 0/F; most active catalysts were Ni on kieselguhr and a novel Raney Ni; 105 references]
Journal Article
·
· Inst. Gas Technol., Res. Bull.
OSTI ID:5309649
- Research Organization:
- Inst. of Gas Technol., Chicago
- OSTI ID:
- 5309649
- Journal Information:
- Inst. Gas Technol., Res. Bull., Vol. 31
- Country of Publication:
- United States
- Language:
- English
Similar Records
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]
Results and analysis of three experiments in a bench-scale tube-wall methanation reactor. [7 references; 5 tables; 13 graphs; Raney Ni catalyst; methanation at 300 psig and 340 and 380/sup 0/C]
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]
Patent
·
Sat Nov 26 00:00:00 EST 1955
·
OSTI ID:5309649
Results and analysis of three experiments in a bench-scale tube-wall methanation reactor. [7 references; 5 tables; 13 graphs; Raney Ni catalyst; methanation at 300 psig and 340 and 380/sup 0/C]
Technical Report
·
Wed Sep 01 00:00:00 EDT 1976
·
OSTI ID:5309649
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:5309649
Related Subjects
01 COAL, LIGNITE, AND PEAT
CATALYSTS
CHEMICAL PREPARATION
FUEL GAS
PRODUCTION
SYNTHESIS GAS
METHANATION
COAL
DIATOMACEOUS EARTH
FLUIDIZED BED
HIGH TEMPERATURE
MEDIUM PRESSURE
NICKEL
PILOT PLANTS
POISONING
CARBONACEOUS MATERIALS
CHEMICAL REACTIONS
ELEMENTS
ENERGY SOURCES
FLUIDS
FOSSIL FUELS
FUELS
FUNCTIONAL MODELS
GASES
METALS
SYNTHESIS
TRANSITION ELEMENTS
010404* - Coal
Lignite
& Peat- Gasification
CATALYSTS
CHEMICAL PREPARATION
FUEL GAS
PRODUCTION
SYNTHESIS GAS
METHANATION
COAL
DIATOMACEOUS EARTH
FLUIDIZED BED
HIGH TEMPERATURE
MEDIUM PRESSURE
NICKEL
PILOT PLANTS
POISONING
CARBONACEOUS MATERIALS
CHEMICAL REACTIONS
ELEMENTS
ENERGY SOURCES
FLUIDS
FOSSIL FUELS
FUELS
FUNCTIONAL MODELS
GASES
METALS
SYNTHESIS
TRANSITION ELEMENTS
010404* - Coal
Lignite
& Peat- Gasification