Effect of eccentricity and interaction between kinetics and mass transfer on the behaviour of catalytic annular reactors: a comparison between lumped and distributed models-Reference-Cited by-同舟云学术

Effect of eccentricity and interaction between kinetics and mass transfer on the behaviour of catalytic annular reactors: a comparison between lumped and distributed models

Published:2001-08 Issue:16 Volume:56 Page:4863-4878
ISSN:0009-2509
Container-title:Chemical Engineering Science
language:en
Short-container-title:Chemical Engineering Science

Author:

Papadias D.,Edsberg L.,Björnbom P.

Publisher

Elsevier BV

Subject

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

Reference35 articles.

1. Analysis of a catalytic annular reactor for very short contact times;Beretta;Chemical Engineering Science,1999

2. Potentialities and draw-backs of the experimental approach to the study of high T and high GHSV kinetics;Beretta;Applied Catalysis A: General,1999

3. Stofftransport bei Wandreaktion im Einlaufgebiet eines Strömungsrohres;Bräuer;Chemie Ingenieur Technik,1966

4. On the dynamic behavior of the catalytic fixed-bed reactor in the region of multiple steady states: Part I. The influence of heat conduction in two phase model;Eigenberger;Chemical Engineering Science,1972

5. Dynamic modelling, bifurcation and chaotic behaviour of gas–solid catalytic reactors.;Elnashaie,1996

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2. CFD modeling of mass transfer in annular reactors;International Journal of Heat and Mass Transfer;2009-11

3. Design and characterisation of a close-concentric annular reactor for kinetic studies at high temperatures;Chemical Engineering Science;2002-03