MULTICOMPONENT VAPOR-LIQUID EQUILIBRIA IN MISCIBLE SYSTEMS FROM BINARY PARAMETERS

被引：28
作者：
HUDSON, JW
VANWINKL.M
机构：
来源：
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1970年 / 9卷 / 03期
关键词：
D O I：
10.1021/i260035a016
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
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页码：466 / &
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共 46 条
[1]   METHANOL-ETHANOL-ACETONE - VAPOR-LIQUID EQUILIBRIA [J].
AMER, HH ;
PAXTON, RR ;
VANWINKLE, M .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1956, 48 (01) :142-146
[2]   VAPOR-LIQUID EQUILIBRIA AT 760 MM PRESSURE - 2-PROPANOL-METHANOL, 2-PROPANOL-ETHYL ALCOHOL, 2-PROPANOL-PROPANOL, AND 2-PROPANOL-2-BUTYL ALCOHOL SYSTEMS [J].
BALLARD, LH ;
VANWINKLE, M .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (10) :2450-2453
[3]  
BELKNAP RC, 1961, J CHEM ENG DATA, V6, P485
[4]   SYSTEMATIC PREDICTION OF SEPARATION FACTORS SCREENING ESTIMATES .1. [J].
BLACK, C ;
DERR, EL ;
PAPADOPOULOS, MN .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1963, 55 (08) :40-&
[5]  
BUSHMAKIN YN, 1957, ZH PRIKL KHIM, V30, P200
[6]   Studies in distillation - Liquid-vapor equilibria of ethyl alcohol-water mixtures [J].
Carey, JS ;
Lewis, WK .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1932, 24 :882-883
[7]  
DELZENNE AO, 1958, J CHEM ENG DATA, V3, P224
[8]  
Free K. W., 1959, J CHEM ENG DATA, V4, P193
[9]  
FRESHWATER DC, 1959, J CHEM ENG DATA, V4, P193
[10]   VAPOR-LIQUID EQUILIBRIA OF TERNARY SYSTEM ACETONE-CHLOROFORM-2,3-DIMETHYLBUTANE [J].
GARRETT, GR ;
VANWINKL.M .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1969, 14 (03) :302-&
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