Modelling of gas–liquid reactors — stability and dynamic behaviour of a hydroformylation reactor, influence of mass transfer in the kinetics controlled regime-Reference-Cited by-同舟云学术

Modelling of gas–liquid reactors — stability and dynamic behaviour of a hydroformylation reactor, influence of mass transfer in the kinetics controlled regime

Published:2001-02 Issue:4 Volume:56 Page:1491-1500
ISSN:0009-2509
Container-title:Chemical Engineering Science
language:en
Short-container-title:Chemical Engineering Science

Author:

Van Elk E.P,Borman P.C,Kuipers J.A.M,Versteeg G.F

Publisher

Elsevier BV

Subject

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

Reference8 articles.

1. Modelling of gas–liquid reactors — implementation of the penetration model in dynamic modelling of gas–liquid processes;van Elk;Chemical Engineering Journal,2000

2. Modelling of gas–liquid reactors — stability and dynamic behavior of gas–liquid mass transfer accompanied by irreversible reaction;van Elk;Chemical Engineering Science,1999

3. Design procedure for stable operations of first-order reaction systems in a CSTR;Heiszwolf;A.I.Ch.E. Journal,1997

4. The rate of absorption of a pure gas into a still liquid during short periods of exposure;Higbie;Transactions of the American Institute of Chemical Engineering,1935

5. Steady-state and dynamic behavior of fast gas–liquid reactions in non-adiabatic continuous stirred tank reactors;Huang;Chemical Engineering Journal,1981

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