Kinetic study of magnesite decomposition under different CO2 pressure conditions and its application in CFD modeling

IF 3.7 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Daokuan Cheng , Hanlu Xu , Bai Wang , Liang Zhao , Hui Dong , Zhijun Zhang
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引用次数: 0

Abstract

By systematically investigating the effect of CO2 on magnesite decomposition, it can provide a more accurate reference for the equipment design of magnesite calcination. In this work, thermogravimetric experiments of magnesite pyrolysis in atmospheres with varying CO2 pressures, P(CO2), were performed, and the behavior and kinetic parameters were investigated. A CFD model of the magnesite flash calciner coupled with the kinetic result was then developed. The results of iso-conversional analysis show that the apparent activation energy, E, is significantly increased from 194.49 kJ/mol in N2 to 305.42 kJ/mol in the atmosphere with P(CO2)= 50 kPa, demonstrating the inhibition effect of CO2. The variation in E also suggests that the conventional method struggles to provide a universal kinetic description across different P(CO2). Therefore, an accommodation function should be introduced to parameterize the effect of the pressure term. The modified kinetic analysis yields a universal kinetic equation with E = 255.77 kJ/mol, kinetic model function f(α)= 1-α, and pressure term h(P)= (P0/P)0.355·[1-(P/Peq)1.849]. The parameters obtained from thermogravimetric (TG) and micro fluidized bed reaction analyzer (MFBRA) were integrated into the CFD model, yielding accurate results. This study is expected to provide tools and scientific reference for design and optimization of magnesite calcining equipment.
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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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