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Kinetic and process study of ethanol steam reforming over Ni/Mg(Al)O catalysts: The initial steps

机译:Ni / Mg(Al)O催化剂上乙醇蒸汽重整的动力学和工艺研究:初始步骤

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In this work, a 2 wt.% Ni/Mg(Al)O catalyst was subjected to kinetic studies for the ethanol steam reforming (ESR) reaction at 500 degrees C, with space-time ranging from 0.03 to 0.50 mg min/ml and with P-C2H5OH:P-H2O:P-Inert = 0.0163:0.0500:0.93 (atm) as standard conditions. The results indicate that dehydrogenation and dehydration of ethanol were the predominant reactions. CH3CHO and C2H4 were primary products and formed in parallel on different active sites. H2O and C2H5OH competed for the same active sites on the catalyst surface and the reaction order with respect to H2O was negative. The apparent activation energy for ethanol conversion was 110 kJ/mol. Furthermore, temperature-programmed desorption experiments confirmed the competing adsorption of C2H5OH and H2O. Temperature-programmed deuteration of used catalyst showed that the catalyst contained C2H4, CHx, acetate and carbonate species during ESR reaction. (C) 2015 Elsevier B.V. All rights reserved.
机译:在这项工作中,对2 wt。%Ni / Mg(Al)O催化剂进行了动力学研究,以研究乙醇蒸汽重整(ESR)反应在500摄氏度下的时空范围为0.03至0.50 mg min / ml和标准条件为P-C2H5OH:P-H2O:P-Inert = 0.0163:0.0500:0.93(atm)。结果表明,乙醇的脱氢和脱水是主要反应。 CH3CHO和C2H4是主要产物,在不同的活性位点上平行形成。 H 2 O和C 2 H 5 OH竞争催化剂表面上相同的活性位,并且相对于H 2 O的反应顺序为负。乙醇转化的表观活化能为110kJ / mol。此外,程序升温脱附实验证实了C2H5OH和H2O的竞争性吸附。对用过的催化剂进行程序编程的氘化表明,在ESR反应过程中,该催化剂含有C2H4,CHx,乙酸盐和碳酸盐类。 (C)2015 Elsevier B.V.保留所有权利。

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