A Ni-based catalyst supported by γ-Al2O3 was prepared by impregnation method, and the catalyst was used in a low CO and CO2 concentration methanation system. The effect of temperature, pressure and space velocity on the methanation reaction was investigated in an experimental fixed-bed reactor. The methanation reaction was operated at the conditions of 190-240°C, 3000-24000ml•g-1•h-1 and 1.5-3.5MPa. The results show that temperature and space velocity play important role on the reaction. With the increase of reaction temperature the CO and CO2 conversion increase and the selectivity of CH4 increase. And with the increase of the space velocity the conversion of CO and CO2 and the selectivity of CH4 decrease sharply
In this study, the Taguchi experimental design method using an L16 orthogonal array was attempted in...
Ni/Al2O3 catalysts (noted as Ni/Al-350, Ni/Al-500, and Ni/Al-700, respectively) were synthesized by ...
The intrinsic kinetics of CO2 methanation over an industrial nickel-based catalyst was determined fo...
A Ni-based catalyst supported by γ-Al2O3 was prepared by impregnation method, and the catalyst was u...
The methanation of CO2 was investigated over a wide range of partial pressures of products and react...
A series of Ni based catalysts prepared by incipient wetness method were characterized by chemisorpt...
The methanation of carbon dioxide under atmospheric pressure on a Co-Ni/Al2O3 catalyst containing 5 ...
International audienceCO2 methanation is one of the most promising ways to store energy based on the...
The methanation of CO₂ was investigated over a wide range of partial pressures of products and react...
CO methanation reaction over the Ni/Al2O3 catalysts for synthetic natural gas production was systema...
AbstractThe aim of this study is to develop an experimental scheme for realization of methanation re...
The catalytic performance of a Ni/Al hydrotalcite derived catalyst for CO2 methanation was analysed ...
Methanation of carbon oxides (CO and CO2) was studied over Ni-based catalysts supported on CeO2, Al2...
The methanation of carbon dioxide has been studied over 3% Ru/Al2O3 and 20% Ni/Al2O3 commercial cata...
The performance characteristics of isothermal fluidized bed syngas methanation for substitute natura...
In this study, the Taguchi experimental design method using an L16 orthogonal array was attempted in...
Ni/Al2O3 catalysts (noted as Ni/Al-350, Ni/Al-500, and Ni/Al-700, respectively) were synthesized by ...
The intrinsic kinetics of CO2 methanation over an industrial nickel-based catalyst was determined fo...
A Ni-based catalyst supported by γ-Al2O3 was prepared by impregnation method, and the catalyst was u...
The methanation of CO2 was investigated over a wide range of partial pressures of products and react...
A series of Ni based catalysts prepared by incipient wetness method were characterized by chemisorpt...
The methanation of carbon dioxide under atmospheric pressure on a Co-Ni/Al2O3 catalyst containing 5 ...
International audienceCO2 methanation is one of the most promising ways to store energy based on the...
The methanation of CO₂ was investigated over a wide range of partial pressures of products and react...
CO methanation reaction over the Ni/Al2O3 catalysts for synthetic natural gas production was systema...
AbstractThe aim of this study is to develop an experimental scheme for realization of methanation re...
The catalytic performance of a Ni/Al hydrotalcite derived catalyst for CO2 methanation was analysed ...
Methanation of carbon oxides (CO and CO2) was studied over Ni-based catalysts supported on CeO2, Al2...
The methanation of carbon dioxide has been studied over 3% Ru/Al2O3 and 20% Ni/Al2O3 commercial cata...
The performance characteristics of isothermal fluidized bed syngas methanation for substitute natura...
In this study, the Taguchi experimental design method using an L16 orthogonal array was attempted in...
Ni/Al2O3 catalysts (noted as Ni/Al-350, Ni/Al-500, and Ni/Al-700, respectively) were synthesized by ...
The intrinsic kinetics of CO2 methanation over an industrial nickel-based catalyst was determined fo...