作者: S. Freni , N. Mondello , S. Cavallaro , G. Cacciola , V.N. Parmon
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摘要: A two-layer fixed-bed catalytic reactor for hydrogen production by steam reforming of ethanol is proposed. In this first converted to acetaldehyde over a Cu-based catalyst and then hydrogen-rich mixture Ni-based catalyst. It shown that the use such type prevents coke formation provides yields closed equilibrium.