PREDICTION OF TERNARY LIQUID - LIQUID EQUILIBRIUM FROM BINARY DATA

被引：34

作者：

MARINA, JM ^{[1
]}

TASSIOS, DP ^{[1
]}

机构：

[1] NEWARK COLL ENGN,NEWARK,NJ 07102

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1973年 / 12卷 / 03期

关键词：

D O I：

10.1021/i260047a010

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：271 / 274

页数：4

共 13 条

[1] A new method for determining dineric distribution [J].

Bancroft, WD ;

Hubard, SS .

JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1942, 64 :347-353

[2]

GARDNER RS, 1967, 2698 US NAV ORDN TES

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

GRISWOLD, J ;

CHU, PL ;

WINSAUER, WO .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (10) :2352-2358

[4]

H?la E., 1968, VAPOR LIQUID EQUILIB

[5] CALCULATION OF TERNARY LIQUID-LIQUID EQUILIBRIA [J].

JOY, DS ;

KYLE, BG .

AICHE JOURNAL, 1969, 15 (02) :298-&

[6]

KATAYAMA T, 1965, AICHE J, V11, P925

[7] EFFECTIVE LOCAL COMPOSITIONS IN PHASE EQUILIBRIUM CORRELATIONS [J].

MARINA, JM ;

TASSIOS, DP .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1973, 12 (01) :67-71

[8] TERNARY SOLUBILITY DATA FOR SYSTEMS INVOLVING 1-PROPANOL AND WATER [J].

MCCANTS, JF ;

JONES, JH ;

HOPSON, WH .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (02) :454-456

[9] PREDICTION OF LIQUID-LIQUID PHASE EQUILIBRIA [J].

PENNINGTON, EN ;

MARWIL, SJ .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (06) :1371-1377

[10] LOCAL COMPOSITIONS IN THERMODYNAMIC EXCESS FUNCTIONS FOR LIQUID MIXTURES [J].

RENON, H ;

PRAUSNITZ, JM .

AICHE JOURNAL, 1968, 14 (01) :135-+

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