Carbon formation on Ni/gamma-Al2O3 catalysts and its kinetics during methane reforming with carbon dioxide was studied in the temperature range of 500-700 degrees C using a thermogravimetric analysis technique. The activation energies of methane cracking, carbon gasification in CO2, as well as carbon deposition in CO2-CH4 reforming were obtained. The results show that the activation energy for carbon gasification is larger than that of carbon formation in methane cracking and that the activation energy of coking in CO2-CH4 reforming is also larger than that of methane decomposition to carbon. The dependencies of coking rate on partial pressures of CH4 and CO2 indicate that methane decomposition is the main route for carbon deposition. A mec...
The CO2 reforming of coke oven gas for the production of synthesis gas has been studied over an acti...
The CO2 reforming of methane is studied over a 20 wt% Ni/USY-zeolite, and more specifically, a therm...
The catalytic activities of Ni/gamma-Al2O3 catalysts prepared using different nickel precursor compo...
An investigation was made using a continuous fixed bed reactor to understand the influence of carbon...
Coke formation in the dry reforming of methane was studied using a thermobalance (TG) and with a cat...
The nature of activation of methane on supported nickel catalyst has been investigated by means of t...
The morphology and properties of the carbon deposition of the nickel-based catalysts for carbon diox...
Carbon dioxide reforming of methane produces synthesis gas with a low hydrogen to carbon monoxide ra...
Major problem in CO 2 reforming of methane (CORM) process is coke formation which is a carbonaceous ...
Carbon dioxide reforming of methane to synthesis gas over Ni supported alumina catalysts was investi...
Major problem in CO2 reforming of methane (CORM) process is coke formation which is a carbonaceous r...
Carbon dioxide reforming of methane to synthesis gas at 750–C over 5 wt % Ni/CaO–Al2O3 catalysts has...
In this paper, a fixed-bed reactor is used to study the influence of different conditions on carbon ...
The relation between coke formation and the deactivation of supported Pt catalysts during CO2 reform...
Oxidative carbon dioxide reforming of methane to synthesis gas over alumina-supported Ni catalysts w...
The CO2 reforming of coke oven gas for the production of synthesis gas has been studied over an acti...
The CO2 reforming of methane is studied over a 20 wt% Ni/USY-zeolite, and more specifically, a therm...
The catalytic activities of Ni/gamma-Al2O3 catalysts prepared using different nickel precursor compo...
An investigation was made using a continuous fixed bed reactor to understand the influence of carbon...
Coke formation in the dry reforming of methane was studied using a thermobalance (TG) and with a cat...
The nature of activation of methane on supported nickel catalyst has been investigated by means of t...
The morphology and properties of the carbon deposition of the nickel-based catalysts for carbon diox...
Carbon dioxide reforming of methane produces synthesis gas with a low hydrogen to carbon monoxide ra...
Major problem in CO 2 reforming of methane (CORM) process is coke formation which is a carbonaceous ...
Carbon dioxide reforming of methane to synthesis gas over Ni supported alumina catalysts was investi...
Major problem in CO2 reforming of methane (CORM) process is coke formation which is a carbonaceous r...
Carbon dioxide reforming of methane to synthesis gas at 750–C over 5 wt % Ni/CaO–Al2O3 catalysts has...
In this paper, a fixed-bed reactor is used to study the influence of different conditions on carbon ...
The relation between coke formation and the deactivation of supported Pt catalysts during CO2 reform...
Oxidative carbon dioxide reforming of methane to synthesis gas over alumina-supported Ni catalysts w...
The CO2 reforming of coke oven gas for the production of synthesis gas has been studied over an acti...
The CO2 reforming of methane is studied over a 20 wt% Ni/USY-zeolite, and more specifically, a therm...
The catalytic activities of Ni/gamma-Al2O3 catalysts prepared using different nickel precursor compo...