Catalytic reforming of methane with carbon dioxide was studied in a fixed-bed reactor using unpromoted and promoted Ni/-Al2O3 catalysts. The effects of promoters, such as alkali metal oxide (Na2O), alkaline-earth metal oxides (MgO, CaO) and rare-earth metal oxides (La2O3, CeO2), on the catalytic activity and stability in terms of coking resistance and coke reactivity were systematically examined. CaO-, La2O3- and CeO2-promoted Ni/-Al2O3 catalysts exhibited higher stability whereas MgO- and Na2O-promoted catalysts demonstrated lower activity and significant deactivation. Metal-oxide promoters (Na2O, MgO, La2O3, and CeO2) suppressed the carbon deposition, primarily due to the enhanced basicities of the supports and highly reactive carbon spec...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
The catalytic activities of Ni/gamma-Al2O3 catalysts prepared using different nickel precursor compo...
Catalytic reforming of methane with carbon dioxide was studied in a fixed-bed reactor using unpromot...
CO2 reforming of methane was studied over modified Ni/Al2O3 catalysts. The metal modifiers were Co, ...
Industrial-scale reforming of methane is typically carried out with an excess of oxidant to suppress...
The effects of active components, promoters and reforming reaction on structure variation of catalys...
Ni catalysts supported on gamma-Al2O3, CeO2 and CeO2-A1(2)O(3) systems were tested for catalytic CO2...
The effects of the support phase and catalyst preparation methods on catalytic activity and carbon d...
Synthesis gas is an important feed stock for the chemical and petrochemical industries to produce ma...
Based on previous observation that the addition of manganese onto Ni/Al2O3 catalysts reduced the cok...
The carbon dioxide reforming of methane was carried out over nickel catalysts supported on the gamma...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
The catalytic activities of Ni/gamma-Al2O3 catalysts prepared using different nickel precursor compo...
Catalytic reforming of methane with carbon dioxide was studied in a fixed-bed reactor using unpromot...
CO2 reforming of methane was studied over modified Ni/Al2O3 catalysts. The metal modifiers were Co, ...
Industrial-scale reforming of methane is typically carried out with an excess of oxidant to suppress...
The effects of active components, promoters and reforming reaction on structure variation of catalys...
Ni catalysts supported on gamma-Al2O3, CeO2 and CeO2-A1(2)O(3) systems were tested for catalytic CO2...
The effects of the support phase and catalyst preparation methods on catalytic activity and carbon d...
Synthesis gas is an important feed stock for the chemical and petrochemical industries to produce ma...
Based on previous observation that the addition of manganese onto Ni/Al2O3 catalysts reduced the cok...
The carbon dioxide reforming of methane was carried out over nickel catalysts supported on the gamma...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
Coke deposition is one of the main challenges in the commercialisation of dry reforming of methane o...
The catalytic activities of Ni/gamma-Al2O3 catalysts prepared using different nickel precursor compo...