Wall-to-particle heat transfer in steam reformer tubes: CFD comparison of catalyst particles-Reference-Cited by-同舟云学术

Wall-to-particle heat transfer in steam reformer tubes: CFD comparison of catalyst particles

Published:2008-04 Issue:8 Volume:63 Page:2219-2224
ISSN:0009-2509
Container-title:Chemical Engineering Science
language:en
Short-container-title:Chemical Engineering Science

Author:

Dixon Anthony G.,Ertan Taskin M.,Nijemeisland Michiel,Stitt E. Hugh

Publisher

Elsevier BV

Subject

Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference26 articles.

1. Effective radial thermal conductivity of packings in gas flow. Part I convective transport coefficient;Bauer;International Chemical Engineering,1978

2. Effect of the geometric characteristics of commercial catalysts for steam reforming;Bruno;The Chemical Engineering Journal,1988

3. CFD modeling and experimental validation of pressure drop and flow profile in a novel structured catalytic reactor packing;Calis;Chemical Engineering Science,2001

4. Wall and particle-shape effects on heat transfer in packed beds;Dixon;Chemical Engineering Communications,1988

5. CFD study of heat transfer near and at the wall of a fixed bed reactor tube—effect of wall conduction;Dixon;Industrial and Engineering Chemistry Research,2005

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