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A critical comparison between the wave model and the standard dispersion model

  • Published:2003-07 Issue:13 Volume:58 Page:2785-2795
  • ISSN:0009-2509
  • Container-title:Chemical Engineering Science
  • language:en
  • Short-container-title:Chemical Engineering Science

Author:

Iordanidis A.A.,van Sint Annaland M.,Kronberg A.E.,Kuipers J.A.M.

Publisher

Elsevier BV

Subject

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

Reference18 articles.

1. Mass dispersion in liquid flow through packed beds;Benneker;Industrial and Engineering Chemical Research,2002

2. Continuous flow systems. Distribution of residence times;Danckwerts;Chemical Engineering Science,1953

3. Heat transfer in packed beds of low tube/particle diameter ratio;Dixon;A.C.S. Symposium Series,1978

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

5. Chemical reaction analysis and design;Froment,1979

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1. Effect of radial velocity profiles on axial dispersion in packed beds: Transient formulation;Physics of Fluids;2023-03-01

2. Residence time distribution (RTD) revisited;Chemical Engineering Science;2021-02

3. Risk-Based Decision Making for the Management of Change in Process Plants: Benefits of Integrating Probabilistic and Phenomenological Analysis;Industrial & Engineering Chemistry Research;2017-12-11

4. Fixed-bed gas-solid catalytic reactors;Multiphase Catalytic Reactors;2016-06-24

5. References;Thermodynamic Approaches in Engineering Systems;2016
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