Vapor-liquid equilibria in the systems oxolane plus methyl 1,1-dimethylethyl ether and oxolane plus 2-propanol

被引：3

作者：

Wisniak, J

机构：

[1] Department of Chemical Engineering, Ben-Gurion University of the Negev, Beer-Sheva

来源：

JOURNAL OF CHEMICAL AND ENGINEERING DATA | 1997年 / 42卷 / 04期

关键词：

D O I：

10.1021/je960401n

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Vapor-liquid equilibrium at 94 kPa has been determined for the binary systems of oxolane (tetrahydrofuran) with methyl 1,1-dimethylethyl ether (MTBE) and 2-propanol. Both systems deviate slightly from ideal behavior and do not present an azeotrope. The activity coefficients and boiling point of the solutions were correlated with their composition by the Redlich-Kister, Wohl, Wilson, UNIQUAC, NRTL, and Wisniak-Tamir equations.

引用

页码：677 / 680

页数：4

共 16 条

[1] CRITICAL-TEMPERATURES AND PRESSURES OF 30 ORGANIC COMPOUNDS [J].

AMBROSE, D ;

BRODERICK, BE ;

TOWNSEND, R .

JOURNAL OF APPLIED CHEMISTRY AND BIOTECHNOLOGY, 1974, 24 (06) :359-372

[2]

[Anonymous], 1982, CLASSICAL THERMODYNA

[3]

Fredenslund A., 1977, Vapor -liquid equilibra using UNIFAC

[4] EMPIRICAL CORRELATION OF SECOND VIRIAL COEFFICIENTS FOR VAPOR-LIQUID EQUILIBRIUM CALCULATIONS [J].

OCONNELL, JP ;

PRAUSNIT.JM .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1967, 6 (02) :245-&

[5] ALGEBRAIC REPRESENTATION OF THERMODYNAMIC PROPERTIES AND THE CLASSIFICATION OF SOLUTIONS [J].

REDLICH, O ;

KISTER, AT .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1948, 40 (02) :345-348

[6]

REICH R, 1996, COMMUNICATION

[7]

SHNITKO VA, 1969, ZH PRIKL KHIM, V42, P89

[8]

SHNITKO VA, 1977, MASSOOBMENNYE PROTSE, P6

[9]

*TEX A M U SYST TH, 1974, TRC THERM TABL NONH

[10] VAPOR-LIQUID EQUILIBRIUM .1. APPRAISAL OF DATA REDUCTION METHODS [J].

VANNESS, HC ;

BYER, SM ;

GIBBS, RE .

AICHE JOURNAL, 1973, 19 (02) :238-244

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