Simple high-order approximations for unsteady-state diffusion, adsorption and reaction in a catalyst: A unified method by a continued fraction for slab, cylinder and sphere geometries-Reference-Cited by-同舟云学术

Simple high-order approximations for unsteady-state diffusion, adsorption and reaction in a catalyst: A unified method by a continued fraction for slab, cylinder and sphere geometries

Published:2011-09 Issue:2 Volume:173 Page:644-650
ISSN:1385-8947
Container-title:Chemical Engineering Journal
language:en
Short-container-title:Chemical Engineering Journal

Author:

Lee Jietae,Kim Dong Hyun

Publisher

Elsevier BV

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,Environmental Chemistry,General Chemistry

Reference24 articles.

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2. Modelling of the fixed-bed adsorption of methane/nitrogen mixtures on silicalite pellets;Delgado;Sep. Purif. Technol.,2006

3. Simulation of true moving bed adsorptive reactor: detailed particle model and linear driving force approximations;Gomes;Chem. Eng. Sci.,2007

4. Carbon dioxide–nitrogen separation through adsorption on activated carbon in a fixed bed;Dantas;Chem. Eng. J.,2011

5. Approximations for unsteady-state diffusion and reaction in porous catalyst and their application to packed-bed reactor;Kim;AIChE J.,2008

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