MASS TRANSFER MODEL FOR CATALYST CAPSULE IN CATALYTIC DISTILLATION (Ⅰ) MATHEMATICAL MODEL
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MASS TRANSFER MODEL FOR CATALYST CAPSULE IN CATALYTIC DISTILLATION (Ⅰ) MATHEMATICAL MODEL
CIESC JournalIssue 5, (2002)
作者机构:
1. 福州大学化工系
2. 浙江大学化工系
作者简介:
基金信息:
DOI:
CLC:
Online First:25 May 2002,
Published:25 May 2002
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WU Yanxiang, WANG Liangen, ZHAO Zhishan, et al. MASS TRANSFER MODEL FOR CATALYST CAPSULE IN CATALYTIC DISTILLATION (Ⅰ) MATHEMATICAL MODEL[J]. CIESC Journal, 2002, (5).
DOI:
WU Yanxiang, WANG Liangen, ZHAO Zhishan, et al. MASS TRANSFER MODEL FOR CATALYST CAPSULE IN CATALYTIC DISTILLATION (Ⅰ) MATHEMATICAL MODEL[J]. CIESC Journal, 2002, (5).DOI:
MASS TRANSFER MODEL FOR CATALYST CAPSULE IN CATALYTIC DISTILLATION (Ⅰ) MATHEMATICAL MODEL
The mass transfer in catalyst capsule is analysed.It is pointed out that the wetting incompletion of catalyst beads and the concentration gradient within the catalyst capsule reduce catalyst efficiency.The effectiveness factor of catalyst capsule equals to the product of η s and η c.The former
the effective wetting rate of catalyst beads
represents the influences of wetting incompletion of catalyst on catalyst efficiency
the latter represents that of concentration gradient.A two- dimensional model is established and an equation to calculate η c is given.It is indicated that η c is influenced not only by radial diffusion
but also by axial liquid flow.The influence of diffusion resistance on effectiveness factor is greatly weakened by axial liquid flow.