CFD modelling and experimental validation of particle-to-fluid mass and heat transfer in a packed bed at very low channel to particle diameter ratio

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作者：
机构：
[1] Romkes, S.J.P.
[2] Dautzenberg, F.M.
[3] van den Bleek, C.M.
[4] Calis, H.P.A.
来源：
Calis, H.P.A. (h.p.calis@tnw.tudelft.nl) | 1600年 / Elsevier卷 / 96期
关键词：
Catalysis - Heat transfer - Mass transfer - Packed beds - Pressure drop;
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摘要：
In this paper, the mass and heat transfer characteristics of a composite structured catalytic reactor packing (Composite Structured Packing (CSP)) are investigated. A CSP consists of a multichannel framework filled with ordinary catalyst particles, with a square channel-to-particle-diameter ratio (N) of 11+c2RenPr1/3 were obtained by fitting the CFD results for N = 1.00, 1.15, 1.47, 2.00A and 2.00B. © 2003 Elsevier B.V. All rights reserved.
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