Isobaric vapour-liquid equilibria in the ternary system methanol-propyl bromide-toluene and propyl bromide-acetonitrile-toluene

Jaime Wisniak; Abraham Tamir

Isobaric vapour-liquid equilibria in the ternary system methanol-propyl bromide-toluene and propyl bromide-acetonitrile-toluene

Department of Chemical Engineering

Research output: Contribution to journal › Article › peer-review

Abstract

Vapour-liquid equilibrium at 101.3 kPa has been determined for the title systems. The data were correlated by the Redlich-Kister and Wisniak-Tamir equations and the appropriate parameters are reported. The activity coefficients of the ternary systems can be predicted from those of the pertinent binary systems. No ternary azeotrope is present.

Original language	English
Pages (from-to)	245-251
Number of pages	7
Journal	Indian Journal of Technology
Volume	30
Issue number	5
State	Published - 1992

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title = "Isobaric vapour-liquid equilibria in the ternary system methanol-propyl bromide-toluene and propyl bromide-acetonitrile-toluene",

abstract = "Vapour-liquid equilibrium at 101.3 kPa has been determined for the title systems. The data were correlated by the Redlich-Kister and Wisniak-Tamir equations and the appropriate parameters are reported. The activity coefficients of the ternary systems can be predicted from those of the pertinent binary systems. No ternary azeotrope is present. ",

author = "Jaime Wisniak and Abraham Tamir",

year = "1992",

language = "English",

volume = "30",

pages = "245--251",

journal = "Indian Journal of Technology",

issn = "0019-5669",

publisher = "Council of Scientific and Industrial Research",

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T1 - Isobaric vapour-liquid equilibria in the ternary system methanol-propyl bromide-toluene and propyl bromide-acetonitrile-toluene

AU - Wisniak, Jaime

AU - Tamir, Abraham

PY - 1992

Y1 - 1992

N2 - Vapour-liquid equilibrium at 101.3 kPa has been determined for the title systems. The data were correlated by the Redlich-Kister and Wisniak-Tamir equations and the appropriate parameters are reported. The activity coefficients of the ternary systems can be predicted from those of the pertinent binary systems. No ternary azeotrope is present.

AB - Vapour-liquid equilibrium at 101.3 kPa has been determined for the title systems. The data were correlated by the Redlich-Kister and Wisniak-Tamir equations and the appropriate parameters are reported. The activity coefficients of the ternary systems can be predicted from those of the pertinent binary systems. No ternary azeotrope is present.

M3 - Article

SN - 0019-5669

VL - 30

SP - 245

EP - 251

JO - Indian Journal of Technology

JF - Indian Journal of Technology

IS - 5

ER -

Isobaric vapour-liquid equilibria in the ternary system methanol-propyl bromide-toluene and propyl bromide-acetonitrile-toluene

Abstract

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