Journal ArticleDOI
Theoretical analysis of a packed bed membrane reactor
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TLDR
In this paper, an annular reactor packed with matrices in which the catalysts/enzyme/microorganisms are immobilized, has been simulated and the results indicate that the overall resistance and hence the conversion depend upon the Thiele modulus and another parameter, α.About:
This article is published in Chemical Engineering Journal.The article was published on 2001-12-15. It has received 1 citations till now. The article focuses on the topics: Thiele modulus & Packed bed.read more
Citations
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Continuous esterification to produce biodiesel by SPES/PES/NWF composite catalytic membrane in flow-through membrane reactor: Experimental and kinetic studies
Wenying Shi,Benqiao He,Yuping Cao,Jianxin Li,Feng Yan,Zhenyu Cui,Zhiqun Zou,Shiwei Guo,Xiaomin Qian +8 more
TL;DR: The results showed that the CCM structure had a significant effect on the acid conversion, and the conversions obtained from the model are in good agreement with the experimental data.
References
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Journal ArticleDOI
Artificial membranes as carriers for the immobilization of biocatalysts
TL;DR: Artificial membranes, due to their interesting properties (high surface area per unit volume, possibility to combine separation with chemical reaction etc).
Journal ArticleDOI
Packed bed catalytic membrane reactors
TL;DR: In this article, a general catalytic packed bed membrane reactor model was proposed for the thermodynamic properties of the thermodynamics of the steam reforming and the ethane dehydrogenation.
Journal ArticleDOI
An improved theoretical model for hollow-fiber enzyme reactors
Shin-Seung Kim,David O. Cooney +1 more
TL;DR: In this paper, an analysis of hollow-fiber enzyme reactors is presented, for first-order kinetics, which leads to explicit expressions for the concentration fields on both the enzyme and substrate sides.
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Zeolite membrane reactor for isobutane dehydrogenation : Experimental results and theoretical modelling
TL;DR: In this paper, a packed-bed zeolite membrane reactor using Pt-In catalyst was used for dehydrogenation of isobutane, and two sweeping modes were studied, namely the co-current and the countercurrent modes.
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Ethylene epoxidation in a catalytic packed-bed membrane reactor
TL;DR: In this paper, the performance of different membrane reactors for the epoxidation of ethylene was compared with that of a conventional fixed-bed reactor (FBR), under identical overall reaction conditions, using a cesium-doped silver catalyst supported on α-alumina.