VAPOR-LIQUID-EQUILIBRIUM DATA FOR BINARY-SYSTEMS OF CHLOROBENZENE WITH ACETONE, ACETONITRILE, ETHYL-ACETATE, ETHYLBENZENE, METHANOL, AND 1-PENTENE

被引:26
作者
MAHER, PJ [1 ]
SMITH, BD [1 ]
机构
[1] WASHINGTON UNIV,THERMODYNAM RES LAB,ST LOUIS,MO 63130
关键词
D O I
10.1021/je60083a011
中图分类号
O414.1 [热力学];
学科分类号
摘要
Total pressure vapor-liquid equilibrium data were measured for the following six binaries containing chlorobenzene: acetone + chlorobenzene at 313.15, 353.00, and 386.66 K; acetonitrile + chlorobenzene at 293.15, 343.15, and 393.15 K; ethyl acetate + chlorobenzene at 313.15, 353.15, and 393.15; chlorobenzene + ethylbenzene at 293.15 K; methanol + chlorobenzene at 293.15, 338.15, and 385.15 K; 1-pentene + chlorobenzene at 280.00, 320.00, and 360.00 K. The P, T, x data were reduced to y, γ, and GE values by the Mixon-Gumowski-Carpenter method. The vlrlal equation of state truncated after the second coefficient was used to calculate the vapor-phase fugacity coefficients. The Tsonopoulos correlation was used to predict the second vlrlal coefficients. © 1979, American Chemical Society. All rights reserved.
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页码:363 / 377
页数:15
相关论文
共 3 条
[1]   NEW TOTAL PRESSURE VAPOR-LIQUID-EQUILIBRIUM APPARATUS - ETHANOL + ANILINE SYSTEM AT 313.15, 350.81, AND 386.67-K [J].
MAHER, PJ ;
SMITH, BD .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1979, 24 (01) :16-22
[2]   COMPUTATION OF VAPOR-LIQUID EQUILIBRIUM DATA FROM SOLUTION VAPOR PRESSURE MEASUREMENTS [J].
MIXON, FO ;
GUMOWSKI, B ;
CARPENTE.BH .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1965, 4 (04) :455-&
[3]   EMPIRICAL CORRELATION OF SECOND VIRIAL-COEFFICIENTS [J].
TSONOPOULOS, C .
AICHE JOURNAL, 1974, 20 (02) :263-272