PREDICTION OF ACTIVITY COEFFICIENTS AT INFINITE DILUTION

被引：36

作者：

ELLIS, SRM

JONAH, DA

机构：

来源：

CHEMICAL ENGINEERING SCIENCE | 1962年 / 17卷 / 12期

关键词：

D O I：

10.1016/0009-2509(62)80075-X

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

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页码：971 / 976

页数：6

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[1] VAPOR-LIQUID EQUILIBRIA AT SUBATMOSPHERIC PRESSURES - BINARY SYSTEM ACETONE CARBON TETRACHLORIDE
BACHMAN, KC
SIMONS, EL
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (01): : 202 - 205
[2] LIQUID-VAPOUR EQUILIBRIA .8. THE SYSTEMS ACETONE + BENZENE AND ACETONE + CARBON TETRACHLORIDE AT 45-DEGREES-C
BROWN, I
SMITH, F
[J]. AUSTRALIAN JOURNAL OF CHEMISTRY, 1957, 10 (04) : 423 - 428
[3] HEATS OF MIXING .2. ACETONITRILE AND NITROMETHANE SYSTEMS
BROWN, I
FOCK, W
[J]. AUSTRALIAN JOURNAL OF CHEMISTRY, 1956, 9 (02) : 180 - 183
[4] CAUTREAUX M, 1955, AICHE J, V1, P496
[5] VAPOUR LIQUID EQUILIBRIA AT REDUCED PRESSURES - NORMAL-BUTANOL ETHYL BENZENE - ANILINE PARA-CYMENE
ELLIS, SRM
RAZAVIPOUR, M
[J]. CHEMICAL ENGINEERING SCIENCE, 1959, 11 (02) : 99 - 107
[6] ELLIS SRM, 1954, CHEM IND-LONDON, P237
[7] HALA E, 1958, VAPOUR LIQUID EQUILI
[8] JONAH DA, 1961, THESIS BIRMINGHAM U
[9] Calculation of partial pressures of binary mixtures
Levy, RM
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1941, 33 : 928 - 931
[10] THERMODYNAMICS OF NONELECTROLYTE SOLUTIONS - X-Y-T RELATIONS IN A BINARY SYSTEM
REDLICH, O
KISTER, AT
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1948, 40 (02): : 341 - 345