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• W2007402413 abstract "In this study, glycerol, with its high H/C ratio feature, was steam reformed with oxygen to produce hydrogen in packed-bed and Pd/Ag membrane reactors. The addition of oxygen, which causes the partial oxidation, was to achieve thermal neutral for the energy saving purposes. Ni/CeO2/Al2O3 catalyst was used to catalyze the reforming reaction at varying temperature, WHSV, WGMR and O2/C3H8O3 ratios. In the packed-bed runs, the glycerol conversion achieved to 99.56% at temperature of 973 K, WHSV of 5 h−1, WGMR of 9 and O2/C3H8O3 of 0.15. Moreover, the best hydrogen yield was 85.26% at conditions of 773 K, WHSV of 5 h−1, WGMR of 9 and O2/C3H8O3 of 0.15. Besides, the Pd/Ag alloy membrane was also employed for comparative purposes. In the Pd/Ag membrane reactor runs, the results shows that glycerol conversion increased with increasing pressure, but the hydrogen yield also declined. The thermal dynamic simulation is also done with MATLAB software." @default.
• W2007402413 created "2016-06-24" @default.
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• W2007402413 date "2013-09-01" @default.
• W2007402413 modified "2023-10-17" @default.
• W2007402413 title "Autothermal steam reforming of glycerol for hydrogen production over packed-bed and Pd/Ag alloy membrane reactors" @default.
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• W2007402413 doi "https://doi.org/10.1016/j.ijhydene.2013.04.134" @default.
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