Hydrogen was produced by methanol decomposition over cold-rolled foils of intermetallic compound Ni3Al which is known as an excellent high-temperature structural material. We found high catalytic activity and selectivity for methanol decomposition in flat cold-rolled Ni3Al foils. The catalytic activity was enhanced above 713 K by the spontaneous fo...
Hydrogen was produced by methanol decomposition over cold-rolled foils of intermetallic compound Ni3Al which is known as an excellent high-temperature structural material. We found high catalytic activity and selectivity for methanol decomposition in flat cold-rolled Ni3Al foils. The catalytic activity was enhanced above 713 K by the spontaneous fo...
Published in Catalysis Letters
Hydrogen was produced by methanol decomposition over cold-rolled foils of intermetallic compound Ni3Al which is known as an excellent high-temperature structural material. We found high catalytic activity and selectivity for methanol decomposition in flat cold-rolled Ni3Al foils. The catalytic activity was enhanced above 713 K by the spontaneous fo...
Methanol decomposition was carried out over flat cold-rolled foils of intermetallic compound Ni3Al in a temperature range 513-793 K. The methanol decomposition into H-2 and CO was effectively catalyzed at 713-793 K, without any need for coating catalyst layers on the foil surface before reaction. Both catalytic activity and selectivity to H-2 and C...
Methanol decomposition was carried out over flat cold-rolled foils of intermetallic compound Ni3Al in a temperature range 513-793 K. The methanol decomposition into H-2 and CO was effectively catalyzed at 713-793 K, without any need for coating catalyst layers on the foil surface before reaction. Both catalytic activity and selectivity to H-2 and C...
Methanol decomposition was carried out over flat cold-rolled foils of intermetallic compound Ni3Al in a temperature range 513-793 K. The methanol decomposition into H-2 and CO was effectively catalyzed at 713-793 K, without any need for coating catalyst layers on the foil surface before reaction. Both catalytic activity and selectivity to H-2 and C...
Catalysts with various nickel loads were prepared on supports of ZrO2, ZrO2-Y2O3 and ZrO2-CaO, characterized by XRD and TPR and tested for activity in ethanol steam reforming. XRD of the supports identified the monoclinic crystalline phase in the ZrO2 and cubic phases in the ZrO2-Y2O3 and ZrO2-CaO supports. In the catalysts, the nickel impregnated ...
Catalysts with various nickel loads were prepared on supports of ZrO2, ZrO2-Y2O3 and ZrO2-CaO, characterized by XRD and TPR and tested for activity in ethanol steam reforming. XRD of the supports identified the monoclinic crystalline phase in the ZrO2 and cubic phases in the ZrO2-Y2O3 and ZrO2-CaO supports. In the catalysts, the nickel impregnated ...
Catalysts with various nickel loads were prepared on supports of ZrO2, ZrO2-Y2O3 and ZrO2-CaO, characterized by XRD and TPR and tested for activity in ethanol steam reforming. XRD of the supports identified the monoclinic crystalline phase in the ZrO2 and cubic phases in the ZrO2-Y2O3 and ZrO2-CaO supports. In the catalysts, the nickel impregnated ...
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