Ni-based catalysts have been extensively investigated because of their superior catalytic performance. In this study, the Ni-La/Al2O3-CaO-C catalyst was prepared by homogeneous precipitation, employed in the co-pyrolysis of soybean straw with polyethylene to produce hydrogen. The optimal experimental conditions were identified by discussing the carrier synthesis ratio, feedstock ratio, and addition of La. Additionally, the stability of the catalyst was evaluated. It was established that the carrier was produced using a molar ratio, the raw ingredients ratio of 5:5, and that the optimum catalytic action was obtained when La was added. Co-pyrolysis of soybean straw with polyethylene (PE) that was catalyzed by Ni-La/Al2O3-CaO-C generated 55.45...
Hydrogen production from biomass pyrolysis is economically and technologically attractive from the p...
The bi-functional Ni-W@C catalysts were prepared by one-pot reduction-carbonization method and used ...
The influence of catalyst support alumina–silica in terms of different Al₂O₃ to SiO₂ mole ratios con...
Energy security and environmental pollution are two major concerns worldwide. H2 from pyrolysis/gasi...
Abstract A Ni-Mg-Al-Ca catalyst was prepared by a co-precipitation method for hydrogen production fr...
A novel two-stage pyrolysis-plasma/catalysis process has been developed for hydrogen production from...
The different loading of nickel oxide, the effect of the addition of Lanthanum (La) with Al2O3 suppo...
Ni/Pd-co-promoted Al2O3–La2O3 catalysts for selective hydrogen production from polyethylene terephth...
Energy security and environmental pollution have been important topics over the world. With depletio...
Catalytic materials for hydrogen production were synthesized by impregnating waste spruce sawdust wi...
The production of renewable hydrogen-enriched gas from biomass waste is a promising technology for t...
The effect of different pellet sizes of nickel (Ni) and lanthanum (La) promoted Al2O3 support on the...
Energy demand is rising due to worldwide population increase and improvement of living standard. Exc...
Catalytic cracking of volatiles derived from wet pig manure (WPM), dried pig manure and their compos...
The production of hydrogen-enriched syngas from the thermo-chemical conversion of biomass was studie...
Hydrogen production from biomass pyrolysis is economically and technologically attractive from the p...
The bi-functional Ni-W@C catalysts were prepared by one-pot reduction-carbonization method and used ...
The influence of catalyst support alumina–silica in terms of different Al₂O₃ to SiO₂ mole ratios con...
Energy security and environmental pollution are two major concerns worldwide. H2 from pyrolysis/gasi...
Abstract A Ni-Mg-Al-Ca catalyst was prepared by a co-precipitation method for hydrogen production fr...
A novel two-stage pyrolysis-plasma/catalysis process has been developed for hydrogen production from...
The different loading of nickel oxide, the effect of the addition of Lanthanum (La) with Al2O3 suppo...
Ni/Pd-co-promoted Al2O3–La2O3 catalysts for selective hydrogen production from polyethylene terephth...
Energy security and environmental pollution have been important topics over the world. With depletio...
Catalytic materials for hydrogen production were synthesized by impregnating waste spruce sawdust wi...
The production of renewable hydrogen-enriched gas from biomass waste is a promising technology for t...
The effect of different pellet sizes of nickel (Ni) and lanthanum (La) promoted Al2O3 support on the...
Energy demand is rising due to worldwide population increase and improvement of living standard. Exc...
Catalytic cracking of volatiles derived from wet pig manure (WPM), dried pig manure and their compos...
The production of hydrogen-enriched syngas from the thermo-chemical conversion of biomass was studie...
Hydrogen production from biomass pyrolysis is economically and technologically attractive from the p...
The bi-functional Ni-W@C catalysts were prepared by one-pot reduction-carbonization method and used ...
The influence of catalyst support alumina–silica in terms of different Al₂O₃ to SiO₂ mole ratios con...