Mathematical Model of Adsorptive Separation for C_8-Aromatic Hydrocarbon in a Fixed Bed
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Mathematical Model of Adsorptive Separation for C_8-Aromatic Hydrocarbon in a Fixed Bed
CIESC JournalIssue 1, (1986)
作者机构:
华南工学院化学工程研究所,华南工学院化学工程研究所
作者简介:
基金信息:
DOI:
CLC:
Online First:25 March 1986,
Published:25 March 1986
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Lao Miaozhen and Ye Zhenhua(Research Institute of Chemical Engineering, South China Institute of Technology). Mathematical Model of Adsorptive Separation for C_8-Aromatic Hydrocarbon in a Fixed Bed[J]. CIESC Journal, 1986, (1).
DOI:
Lao Miaozhen and Ye Zhenhua(Research Institute of Chemical Engineering, South China Institute of Technology). Mathematical Model of Adsorptive Separation for C_8-Aromatic Hydrocarbon in a Fixed Bed[J]. CIESC Journal, 1986, (1).DOI:
Mathematical Model of Adsorptive Separation for C_8-Aromatic Hydrocarbon in a Fixed Bed
Liquid adsorption in fixed bed was studied at room temperature for the binary system
para-xylene and ethylbenzene
with two types of zeolites- one prepared by our group
and the other imported. The mathematical model included a mass transfer equation involving the total mass transfer coefficient
and the equilibrium and the mass balance equations. These three equations were integrated numerically. The predicted breakthrough curves was close to the experimental. To explore further the mechanism of mass transfer
three models-liquid-phase controlling
solid-phase controlling and both-phase controlling were examined. The results showed that the solid-phase controlling model is the most appropriate for a system studied.