Modeling the Partial Oxidation of o-Xylene in an Industrial Packed-Bed Catalytic Reactor: The Role of Hydrodynamics and Catalyst Activity in the Heat Transport-Reference-Cited by-同舟云学术

Modeling the Partial Oxidation of o-Xylene in an Industrial Packed-Bed Catalytic Reactor: The Role of Hydrodynamics and Catalyst Activity in the Heat Transport

Published:2010-07-28 Issue:15 Volume:49 Page:6845-6853
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Castillo-Araiza C. O.¹,López-Isunza F.¹

Affiliation:

1. Departamento de Ingeniería de Procesos e Hidráulica, Universidad Autónoma Metropolitana—Iztapalapa, Iztapalapa, México 09340 DF

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie901720z

Reference57 articles.

1. Void fraction distribution in beds of spheres

2. Some remarks on channelling and on radial dispersion in packed beds

3. A simple and coherent set of coefficients for modelling of heat and mass transport with and without chemical reaction in tubes filled with spheres

4. Velocity, temperature and conversion profiles in fixed bed catalytic reactors

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