Modelling of the Membrane Permeability Effect on the H2 Production Using CFD Method

被引：4
|
作者：
Benguerba, Yacine [1 ]
Dumas, Christine [2 ]
Ernst, Barbara [2 ]
机构：
[1] Univ Setif1, Lab Genie Procedes Chim, Setif 19000, Algeria
[2] Ecole Europeenne Chim Polymeres & Mat ECPM, LPS, IPHC DSA, ULP,CNRS 7178, F-67087 Strasbourg 2, France
来源：
INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING | 2014年 / 12卷 / 01期
关键词：
Membrane reactor; dense membrane; Porous membrane; CFD; Hydrogen; Permeability; WATER-GAS SHIFT; COMPOSITE MEMBRANE; HYDROGEN; KINETICS; METHANE; REACTOR;
D O I：
10.1515/ijcre-2013-0063
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
Autothermal reforming of CH4 in a membrane catalytic microreactor for the production of hydrogen at different temperatures over supported Ni catalysts has been studied. A three-dimensional mathematical model was developed using a computational fluid dynamics (CFD) technique. The effect of using different membranes on the performance of the micro-reactor was analysed. The amounts of hydrogen produced and separated in each case, under the same operating conditions, were compared. It was proven that using the porous membrane (Ni-Al2O3) could be an economic solution for the production and separation of hydrogen in membrane reactors.
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页数：12
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