A mathematical modeling of catalytic milli-fixed bed reactor for Fischer–Tropsch synthesis: Influence of tube diameter on Fischer Tropsch selectivity and thermal behavior-Reference-Cited by-同舟云学术

A mathematical modeling of catalytic milli-fixed bed reactor for Fischer–Tropsch synthesis: Influence of tube diameter on Fischer Tropsch selectivity and thermal behavior

Published:2015-05 Issue: Volume:127 Page:72-83
ISSN:0009-2509
Container-title:Chemical Engineering Science
language:en
Short-container-title:Chemical Engineering Science

Author:

Chabot Giovanni,Guilet Richard,Cognet Patrick,Gourdon Christophe

Publisher

Elsevier BV

Subject

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

Reference43 articles.

1. Fischer–Tropsch reaction mechanism involving stepwise growth of carbon chain;Anderson;J. Chem. Phys.,1951

2. Kinetics of the Fischer–Tropsch reaction over iron;Atwood;Ind. Eng. Chem. Process Des. Dev.,1979

3. Effective radial thermal conductivity of packing in gas flow. Part I. convective transport coefficient;Bauer;Int. Chem. Eng.,1978

4. Effective radial thermal conductivity of packing in gas flow. Part II. Thermal conductivity of the packing fraction without gas flow;Bauer;Int. Chem. Eng,1978

5. Influence of tube and particle diameter on heat transport in packed beds;Borkink;AIChE J,1992

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