Low metal content Co and Ni alumina supported catalysts (4.0, 2.5 and 1.0 wt% nominal metal content) have been prepared, characterized (by ICP-OES, TEM, TPR-H2 and TPO) and tested for the CO2 reforming of methane. The objective is to optimize the metal loading in order to have a more efficient system. The selected reaction temperature is 973 K, although some tests at higher reaction temperature have been also performed. The results show that the amount of deposited carbon is noticeably lower than that obtained with the Co and Ni reference catalysts (9 wt%), but the CH4 and CO2 conversions are also lower. Among the catalysts tested, the Co(1) catalyst (the value in brackets corresponds to the nominal wt% loading) is deactivated during the fi...
CO2 reforming of methane is attractive, because it can convert two greenhouse gases into synthesis g...
In this study, the potential of dry reforming reaction over CaFe2O4 supported Ni and Co catalysts we...
The catalytic performances of promoter-modified and un-modified bimetallic catalysts in CO2 reformin...
Carbon dioxide reforming of methane to synthesis gas over Ni supported alumina catalysts was investi...
Oxidative carbon dioxide reforming of methane to synthesis gas over alumina-supported Ni catalysts w...
The CO2 reforming of methane to syngas was examined over five different supported catalysts. In this...
CO2 reforming of methane was studied over modified Ni/Al2O3 catalysts. The metal modifiers were Co, ...
Carbon dioxide reforming of methane produces synthesis gas with a low hydrogen to carbon monoxide ra...
Consuming two major greenhouse gases, carbon dioxide (CO2) and methane (CH4), to produce synthesis g...
Reforming of methane with carbon dioxide has recently received an increasing interest since it has s...
The catalytic activities of Ni/gamma-Al2O3 catalysts prepared using different nickel precursor compo...
The effects of the support phase and catalyst preparation methods on catalytic activity and carbon d...
The activity and stability of catalysts for methane-carbon dioxide reforming depend subtly upon the ...
The effect of the TiO2-P25 content on the catalytic performance of Ni/ TiO2-P25– α- Al2O3 for carbo...
The chemical recycling of greenhouse gas CO2 produced in hydrocarbon combustion is an attractive alt...
CO2 reforming of methane is attractive, because it can convert two greenhouse gases into synthesis g...
In this study, the potential of dry reforming reaction over CaFe2O4 supported Ni and Co catalysts we...
The catalytic performances of promoter-modified and un-modified bimetallic catalysts in CO2 reformin...
Carbon dioxide reforming of methane to synthesis gas over Ni supported alumina catalysts was investi...
Oxidative carbon dioxide reforming of methane to synthesis gas over alumina-supported Ni catalysts w...
The CO2 reforming of methane to syngas was examined over five different supported catalysts. In this...
CO2 reforming of methane was studied over modified Ni/Al2O3 catalysts. The metal modifiers were Co, ...
Carbon dioxide reforming of methane produces synthesis gas with a low hydrogen to carbon monoxide ra...
Consuming two major greenhouse gases, carbon dioxide (CO2) and methane (CH4), to produce synthesis g...
Reforming of methane with carbon dioxide has recently received an increasing interest since it has s...
The catalytic activities of Ni/gamma-Al2O3 catalysts prepared using different nickel precursor compo...
The effects of the support phase and catalyst preparation methods on catalytic activity and carbon d...
The activity and stability of catalysts for methane-carbon dioxide reforming depend subtly upon the ...
The effect of the TiO2-P25 content on the catalytic performance of Ni/ TiO2-P25– α- Al2O3 for carbo...
The chemical recycling of greenhouse gas CO2 produced in hydrocarbon combustion is an attractive alt...
CO2 reforming of methane is attractive, because it can convert two greenhouse gases into synthesis g...
In this study, the potential of dry reforming reaction over CaFe2O4 supported Ni and Co catalysts we...
The catalytic performances of promoter-modified and un-modified bimetallic catalysts in CO2 reformin...