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
·
· U. Technol., Bengal Eng. Coll.
OSTI ID:5216868
- Research Organization:
- Bengal Eng. Coll., Howrah, India
- OSTI ID:
- 5216868
- Journal Information:
- U. Technol., Bengal Eng. Coll., Vol. 4
- Country of Publication:
- United States
- Language:
- English
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Coal gas as a substitute for synthesis gas in the Fischer--Tropsch synthesis. [Removal of O from coal gas by passage over Cu turnings at 320-50/sup 0/; gas freed of S by passage over alkalized Fe/sub 2/O/sub 3/ at 250/sup 0/; catalyst of 100 Co, 5 ThO/sub 2/, 8 MgO, 80 kieselguhr]
Coal gas as a substitute for synthesis gas in Fischer--Tropsch reactions. III. [Coal gas (CO/sub 2/ 5. 38, H 25. 9, O 2. 7, CH/sub 4/ 19. 05, unsaturated hydrocarbons 3. 10, C/sub 2/ and higher saturated hydrocarbons 0. 41, CO 7. 25, N 36. 23%) reacted over catalyst (MgO--ThO/sub 2/--kieselguhr)]
Hydrocarbon synthesis. [Passage of synthesis gas successively through catalyst beds at various temperatures; catalyst beds of Ni on Filtercel with oxides of Mn, U, and Th at 360/sup 0/F, Co on Filtercel with MgO and ThO/sub 2/ at 390/sup 0/F, Co on Filtercel with MgO, ThO/sub 2/, and Na/sub 2/CO/sub 3/ at 420/sup 0/F, and Fe on Al/sub 2/O/sub 3/ with Cu and K/sub 2/O at 480/sup 0/F]
Journal Article
·
Tue Jan 01 00:00:00 EST 1957
· J. Technol., Bengal Eng. Coll.
·
OSTI ID:5216868
Coal gas as a substitute for synthesis gas in Fischer--Tropsch reactions. III. [Coal gas (CO/sub 2/ 5. 38, H 25. 9, O 2. 7, CH/sub 4/ 19. 05, unsaturated hydrocarbons 3. 10, C/sub 2/ and higher saturated hydrocarbons 0. 41, CO 7. 25, N 36. 23%) reacted over catalyst (MgO--ThO/sub 2/--kieselguhr)]
Journal Article
·
Fri Jan 01 00:00:00 EST 1960
· J. Technol., Bengal Eng. Coll.
·
OSTI ID:5216868
Hydrocarbon synthesis. [Passage of synthesis gas successively through catalyst beds at various temperatures; catalyst beds of Ni on Filtercel with oxides of Mn, U, and Th at 360/sup 0/F, Co on Filtercel with MgO and ThO/sub 2/ at 390/sup 0/F, Co on Filtercel with MgO, ThO/sub 2/, and Na/sub 2/CO/sub 3/ at 420/sup 0/F, and Fe on Al/sub 2/O/sub 3/ with Cu and K/sub 2/O at 480/sup 0/F]
Patent
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Tue Apr 11 00:00:00 EST 1950
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OSTI ID:5216868