Modeling a Membrane Reformer with a Carbon-Monoxide Conversion Catalyst for Extracting High-Purity Hydrogen from Methane Steam-Conversion Products
- 作者: Vandyshev A.B.1, Kulikov V.A.1
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隶属关系:
- Institute of Engineering Science, Ural Branch, Russian Academy of Sciences
- 期: 卷 54, 编号 5-6 (2018)
- 页面: 313-321
- 栏目: Cryogenic Technology. Production and Use of Industrial Gases. Vacuum Technology
- URL: https://ogarev-online.ru/0009-2355/article/view/236279
- DOI: https://doi.org/10.1007/s10556-018-0481-4
- ID: 236279
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详细
A mathematical model for membrane extraction of high-purity hydrogen from methane steam-conversion products that takes into account hydrogen outflow through a palladium membrane (V-1 alloy) and chemical reactions among components of the starting gas mixture in the presence of a carbon monoxide conversion catalyst is presented. A practical example shows that the presented model describes adequately and rather accurately the main parameters of the model membrane reformer with the carbonmonoxide catalyst and allows the optimal technological regimes to be selected.
作者简介
A. Vandyshev
Institute of Engineering Science, Ural Branch, Russian Academy of Sciences
编辑信件的主要联系方式.
Email: vandyshev@imach.uran.ru
俄罗斯联邦, Ekaterinburg
V. Kulikov
Institute of Engineering Science, Ural Branch, Russian Academy of Sciences
Email: vandyshev@imach.uran.ru
俄罗斯联邦, Ekaterinburg
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