Effect of catalytic combustion of hydrogen on the dehydration processes in a membrane reactor. III. calculation of the industrial reactor
- 作者: Shelepova E.V.1, Vedyagin A.A.1,2, Noskov A.S.1
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隶属关系:
- Boreskov Institute of Catalysis, Siberian Branch
- Tomsk Polytechnic University
- 期: 卷 53, 编号 6 (2017)
- 页面: 626-633
- 栏目: Article
- URL: https://journals.rcsi.science/0010-5082/article/view/152980
- DOI: https://doi.org/10.1134/S0010508217060028
- ID: 152980
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详细
This paper describes the mathematical simulation of an industrial membrane reactor for propane dehydrogenation in the thermodynamic coupling with hydrogen combustion (oxidation). Due to the effective removal of hydrogen through a membrane and the heat release as a result of an exothermic reaction, the temperature of the reaction stream at the input could be reduced to 500◦C. The fact that the process is carried out on an industrial-level membrane reactor makes it possible to reach a propane conversion of 75% with a propylene selectivity of 97%, which exceeds the figures obtained per pass in existing industrial devices at higher temperatures.
作者简介
E. Shelepova
Boreskov Institute of Catalysis, Siberian Branch
编辑信件的主要联系方式.
Email: shev@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090
A. Vedyagin
Boreskov Institute of Catalysis, Siberian Branch; Tomsk Polytechnic University
Email: shev@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090; Tomsk, 634050
A. Noskov
Boreskov Institute of Catalysis, Siberian Branch
Email: shev@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090
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