EVALUATION OF ACTIVITY COEFFICIENTS FROM TERNARY LIQUID-LIQUID EQUILIBRIA

被引：7

作者：

JOY, DS

KYLE, BG

机构：

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1970年 / 9卷 / 02期

关键词：

D O I：

10.1021/i260034a013

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：244 / &

共 13 条

[1]

Akita K., 1963, J CHEM ENG DATA, V8, P484, DOI 10.1021/je60019a003

[2]

BOBERG TC, 1960, THESIS U MICHIGAN

[3] VAPOR-LIQUID-LIQUID EQUILIBRIUM OF N-PENTANE-SULFUR DIOXIDE-BENZENE SYSTEM AT 0 DEGREES F [J].

BOWDEN, WW ;

STATON, JC ;

SMITH, BD .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1966, 11 (03) :296-&

[4] A NEW METHOD OF CONSTRAINED OPTIMIZATION AND A COMPARISON WITH OTHER METHODS [J].

BOX, MJ .

COMPUTER JOURNAL, 1965, 8 (01) :42-52

[5] Dineric distribution [J].

Hand, DB .

JOURNAL OF PHYSICAL CHEMISTRY, 1930, 34 (09) :1961-2000

[6]

HENTY CJ, 1964, J APPL CHEM, V14, P148

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

JOY, DS ;

KYLE, BG .

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

[8]

JOY DS, 1968, THESIS KANSAS STATE

[9] PREDICTION OF TERNARY LIQUID-LIQUID EQUILIBRIUM FROM BINARY DATA (FOR THE SYSTEM FURFURAL ISO-OCTANE BENZENE) [J].

KENNY, JW .

CHEMICAL ENGINEERING SCIENCE, 1957, 6 (03) :116-122

[10] Partial pressures of ternary liquid systems and the prediction of tie lines [J].

Othmer, DF ;

Tobias, PE .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1942, 34 :696-700

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