Effect of hydrogen on carbon deposition from carbon monoxide on nickel catalyst

1994 ◽  
Vol 23 (3-4) ◽  
pp. 237-243 ◽  
Author(s):  
N. Yoshida ◽  
T. Yamamoto ◽  
F. Minoguchi ◽  
S. Kishimoto
Keyword(s):  
Carbon Monoxide ◽  
Nickel Catalyst ◽  
Carbon Deposition

Effect of Nonthermal Plasma on the Methanation of Carbon Monoxide over Nickel Catalyst

2010 ◽  
Vol 30 (4) ◽  
pp. 437-447 ◽  
Author(s):  
Y. S. Mok ◽  
H.-C. Kang ◽  
H.-J. Lee ◽  
D. J. Koh ◽  
D. N. Shin
Keyword(s):  
Carbon Monoxide ◽  
Nickel Catalyst ◽  
Nonthermal Plasma

scholarly journals A study of catalytic actions at solid surfaces. Part IX. — The action of copper in promoting the activity of nickel catalyst

1922 ◽  
Vol 102 (714) ◽  
pp. 27-32 ◽  
Keyword(s):  
Carbon Monoxide ◽  
Nickel Catalyst ◽  
Methyl Alcohol ◽  
Copper Alloy ◽  
Copper Oxides ◽  
Solid Surfaces ◽  
Molybdenum Catalyst ◽  
Silver Copper

One of the most interesting cases of promoter action is that in which a mixture of two substances, each of which functions as a catalyst for the same action, shows greater activity than either constituent alone. Thus in the synthesis of ammonia an iron-molybdenum catalyst is stated to afford greater yields of ammonia than is given by either of the metals alone. Again, the production of formaldehyde from methyl alcohol and air was found by Hochstetter to be more effectively performed in presence of a silver-copper alloy than by either silver or copper alone. Carbon monoxide is oxidised more efficiently in presence of certain mixtures of oxides, for example “hopcalite,” than in presence of the constituent oxides (manganese and copper oxides).

Production of Synthetic Petroleum Fuel Through the Absorption of Atmospheric CO2

2009 ◽  
Author(s):  
Stephen G. Pothier ◽  
David Chichka
Keyword(s):  
Carbon Dioxide ◽  
Carbon Monoxide ◽  
Greenhouse Gas ◽  
Nickel Catalyst ◽  
Cobalt Catalyst ◽  
Petroleum Products ◽  
Hydrogen Generator ◽  
Fischer Tropsch ◽  
Petroleum Fuel ◽  
One Year

This paper describes a theoretical device called a Petroleum Synthesizer, which absorbs the greenhouse gas carbon dioxide from the atmosphere and converts it into a synthetic petroleum fuel. The device has four parts: First, a CO2 Scrubber using sodium carbonate reversibly absorbs CO2 from the atmosphere. Simultaneously, a Hydrogen Generator separates water electrolytically to produce hydrogen (H2). Third, a Carbon Monoxide Generator mixes the H2 and the CO2 over a nickel catalyst, changing the constituents into carbon monoxide (CO) and water. Finally, the CO and additional H2 are combined in a cobalt-catalyst Fischer-Tropsch (F-T) Processor to produce gaseous and liquid petroleum products. Calculations show that one watt of electricity supplied for one year would allow the Synthesizer to create 0.420 kg of petroleum products, and absorb 1.314 kg of CO2 from the atmosphere. An acre of solar voltaic panels powering Synthesizers could produce 46,000 kg, or about 14,000 gallons, of petroleum products per acre per year, and absorb 140,000 kg of CO2. By contrast, an acre of corn produces less than 400 gallons of ethanol per year.

The simultaneous reactions of carbon monoxide and hydrogen on a nickel catalyst

1982 ◽  
Vol 2 (6) ◽  
pp. 347-358
Author(s):  
Albert C. Frost ◽  
Louis F. Elek ◽  
Chang-Lee Yang ◽  
Alan P. Risch ◽  
Jule A. Rabo
Keyword(s):  
Carbon Monoxide ◽  
Nickel Catalyst

Methanation of carbon monoxide and carbon dioxide over nickel catalyst under the transient state

1987 ◽  
Vol 33 (1) ◽  
pp. 179-184 ◽  
Author(s):  
S. Fujita ◽  
H. Terunuma ◽  
H. Kobayashi ◽  
N. Takezawa
Keyword(s):  
Carbon Dioxide ◽  
Carbon Monoxide ◽  
Nickel Catalyst ◽  
Transient State

Methanation of Low Levels of Carbon Monoxide over Nickel Catalyst

1969 ◽  
Vol 8 (4) ◽  
pp. 347-352 ◽  
Author(s):  
S. S. Randhava ◽  
E. H. Camara ◽  
Amirali Rehmat
Keyword(s):  
Carbon Monoxide ◽  
Nickel Catalyst ◽  
Low Levels
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