MASS-TRANSFER IN EXTRACTIVE CHROMATOGRAPHY UNDER CONDITIONS OF LINEAR-PHASE EQUILIBRIUM

被引：0

作者：

KOWALSKI, W ^{[1
]}

机构：

[1] WARSAW POLYTECH INST,INST INZYNIERII CHEM & URZADZEN CIEPLNYCH,PL-00661 WARSAW,POLAND

来源：

INZYNIERIA CHEMICZNA I PROCESOWA | 1991年 / 12卷 / 02期

关键词：

D O I：

暂无

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The mass transfer model was presented for extractive chromatography under conditions of linear phase equilibrium. Mass transfer rate in two phases was described by mass transfer coefficients calculated from empirical correlations. Mass transfer was investigated for xylene-acetone-water system. The experimental and calculated outflow curves were in accord.

引用

页码：301 / 310

页数：10

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