Modeling and parameter estimation of coke combustion kinetics in a glycerol catalytic conversion reactor

Abstract : A two dimensional, heterogeneous model was developed for the simulation of a coked catalyst regeneration fixed-bed reactor in a green acrylics process. A kinetic model which consists of combustion of coke containing carbon, hydrogen and oxygen was derived. The unknown parameters (including the kinetic parameters, initial composition and concentration of coke, heat transfer parameters and catalyst pore diameter) were identified using the results of regeneration experiments with the coke formed in a glycerol dehydration process. Good agreements between the model predictions and experimental results were obtained.
Type de document :
Communication dans un congrès
Gernaey, KV and Huusom, JK and Gani, R. 12TH INTERNATIONAL SYMPOSIUM ON PROCESS SYSTEMS ENGINEERING (PSE) AND 25TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING (ESCAPE), PT A, 2015, Copenhague, Denmark. 37 (A), pp.335-340, 2015, Computer Aided Chemical Engineering
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https://hal.univ-lorraine.fr/hal-01267378
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Soumis le : jeudi 4 février 2016 - 12:42:25
Dernière modification le : jeudi 11 janvier 2018 - 06:25:27

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  • HAL Id : hal-01267378, version 1

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Minghai Lei, François Lesage, M. Abderrazak Latifi, Serge Tretjak. Modeling and parameter estimation of coke combustion kinetics in a glycerol catalytic conversion reactor. Gernaey, KV and Huusom, JK and Gani, R. 12TH INTERNATIONAL SYMPOSIUM ON PROCESS SYSTEMS ENGINEERING (PSE) AND 25TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING (ESCAPE), PT A, 2015, Copenhague, Denmark. 37 (A), pp.335-340, 2015, Computer Aided Chemical Engineering. 〈hal-01267378〉

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