Analysis of the CSTR with Two-Phase Flow under Phase Equilibrium Conditions Full article
Journal |
Chemical Engineering Science
ISSN: 0009-2509 , E-ISSN: 1873-4405 |
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Output data | Year: 2005, Volume: 60, Pages: 3199-3206 Pages count : 8 DOI: 10.1016/j.ces.2005.01.001 | ||
Tags | Mathematical modeling, Multiphase reactions, Phase equilibria, Thermodynamics process | ||
Authors |
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Abstract:
A mathematical model of the flow gas–liquid continuous stirred tank reactor (CSTR) is presented under the assumption of thermodynamic equilibrium of the two-phase flow. Phase equilibrium was calculated using the Redlich–Kwong–Soave (RKS) equation of state. An efficient algorithm based on homotopymethod was used to obtain a numerical solution of the system of nonlinear algebraic equations of the model. Byan example of the liquid-phase hydrogenation of benzene, steadystates were analyzed in isothermal and adiabatic regimes and at
partial removal of heat released as a result of exothermic reaction. It was shown that under certain conditions, a multiplicityof stationary solutions is possible due to nonlinearityof the kinetic reaction, on the one hand, and deviation of the reaction mixture properties from the ideal state, on the other hand
Cite:
Yermakova A.
, Anikeev V.I.
Analysis of the CSTR with Two-Phase Flow under Phase Equilibrium Conditions
Chemical Engineering Science. 2005. V.60. P.3199-3206. DOI: 10.1016/j.ces.2005.01.001 WOS Scopus РИНЦ
Analysis of the CSTR with Two-Phase Flow under Phase Equilibrium Conditions
Chemical Engineering Science. 2005. V.60. P.3199-3206. DOI: 10.1016/j.ces.2005.01.001 WOS Scopus РИНЦ
Dates:
Submitted: | Feb 28, 2004 |
Accepted: | Jan 11, 2005 |
Published online: | Mar 4, 2005 |
Published print: | Jun 1, 2005 |
Identifiers:
Web of science | WOS:000229203300004 |
Scopus | 2-s2.0-17544375370 |
Elibrary | 13484061 |
Chemical Abstracts | 2005:366913 |
Chemical Abstracts (print) | 142:448791 |
OpenAlex | W2169798848 |