ESTIMATION OF PARAMETERS FOR NRTL EQUATION FOR EXCESS GIBBS ENERGIES OF STRONGLY NONIDEAL LIQUID MIXTURES

被引：523

作者：

RENON, H

PRAUSNIT.JM

机构：

[1] Department of Chemical Engineering, University of California, Berkeley

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1969年 / 8卷 / 03期

关键词：

D O I：

10.1021/i260031a019

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Charts are given for estimating NRTL (nonrandom, two-liquid) parameters from limiting activity coefficient data or from mutual solubilities. Calculated and experimental results are given for binary and ternary systems. © 1969, American Chemical Society. All rights reserved.

引用

页码：413 / &

共 14 条

[1]

EDWARDS JB, 1962, THESIS GEORGIA I TEC

[2] SEPARATION OF SYNTHESIS MIXTURES - PHASE EQUILIBRIA IN ETHYL ALCOHOL ETHYL ACETATE WATER SYSTEM [J].