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Modelling of a Simulated Moving Bed in case of non-ideal hydrodynamics

  • Published:2016-10 Issue: Volume:153 Page:188-198
  • ISSN:0009-2509
  • Container-title:Chemical Engineering Science
  • language:en
  • Short-container-title:Chemical Engineering Science

Author:

Fangueiro Gomes L.,Augier F.,Leinekugel-le-Cocq D.,Vinkovic I.,Simoëns S.

Publisher

Elsevier BV

Subject

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

Reference45 articles.

1. Augier, F., Hotier, G., 2011. U.S. Patent Application 13/154,874.

2. Application of computational fluid dynamics to fixed bed adsorption calculations: effect of hydrodynamics at laboratory and industrial scale;Augier;Sep. Purif. Technol.,2008

3. Two-dimensional non-isothermal model for toluene adsorption in a fixed-bed adsorber;Bart;Chem. Eng. Process.: Process Intensif.,1996

4. On the modeling of flow in packed bed systems;Benyahia;Part. Sci. Technol.,2004

5. Intensification of paraxylene production using a simulated moving bed reactor;Bergeot;Oil Gas. Sci. Technol. Rev. d’IFPEnergies Nouv.,2010

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