Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6 = Phasengleichgewichte in binären systemen von Methanol mit Sulfolan, Tetraethylenglycoldimethylether und 18-krone-6 Kronenether

M. Kuczynski; W. 't Hart; K.R. Westerterp

doi:10.1016/0255-2701(86)85008-5

Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6 = Phasengleichgewichte in binären systemen von Methanol mit Sulfolan, Tetraethylenglycoldimethylether und 18-krone-6 Kronenether

M. Kuczynski, W. 't Hart, K.R. Westerterp

University of Twente

Research output: Contribution to journal › Article › Academic

6 Citations (Scopus)

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Abstract

The activity coefficients of methanol in sulfolane, tetraethylene glycol dimethyl ether (TEGDME) and 18-crown-6 under conditions of equilibrium have been determined in the temperature range 423–503 K and in the pressure range 0.28–3.5 MPa. A minimum in the activity coefficient was found for the methanol—TEGDME and methanol—18-crown-6 solutions.

Original language	Undefined
Pages (from-to)	53-58
Journal	Chemical engineering and processing : process intensification
Volume	20
Issue number	1
DOIs	https://doi.org/10.1016/0255-2701(86)85008-5
Publication status	Published - 1986

Keywords

IR-69633

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10.1016/0255-2701(86)85008-5

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Cite this

Kuczynski, M., 't Hart, W., & Westerterp, K. R. (1986). Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6 = Phasengleichgewichte in binären systemen von Methanol mit Sulfolan, Tetraethylenglycoldimethylether und 18-krone-6 Kronenether. Chemical engineering and processing : process intensification, 20(1), 53-58. https://doi.org/10.1016/0255-2701(86)85008-5

Kuczynski, M. ; 't Hart, W. ; Westerterp, K.R. / Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6 = Phasengleichgewichte in binären systemen von Methanol mit Sulfolan, Tetraethylenglycoldimethylether und 18-krone-6 Kronenether. In: Chemical engineering and processing : process intensification. 1986 ; Vol. 20, No. 1. pp. 53-58.

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abstract = "The activity coefficients of methanol in sulfolane, tetraethylene glycol dimethyl ether (TEGDME) and 18-crown-6 under conditions of equilibrium have been determined in the temperature range 423–503 K and in the pressure range 0.28–3.5 MPa. A minimum in the activity coefficient was found for the methanol—TEGDME and methanol—18-crown-6 solutions.",

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author = "M. Kuczynski and {'t Hart}, W. and K.R. Westerterp",

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doi = "10.1016/0255-2701(86)85008-5",

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journal = "Chemical engineering and processing : process intensification",

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Kuczynski, M, 't Hart, W & Westerterp, KR 1986, 'Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6 = Phasengleichgewichte in binären systemen von Methanol mit Sulfolan, Tetraethylenglycoldimethylether und 18-krone-6 Kronenether', Chemical engineering and processing : process intensification, vol. 20, no. 1, pp. 53-58. https://doi.org/10.1016/0255-2701(86)85008-5

Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6 = Phasengleichgewichte in binären systemen von Methanol mit Sulfolan, Tetraethylenglycoldimethylether und 18-krone-6 Kronenether. / Kuczynski, M.; 't Hart, W.; Westerterp, K.R.

In: Chemical engineering and processing : process intensification, Vol. 20, No. 1, 1986, p. 53-58.

Research output: Contribution to journal › Article › Academic

TY - JOUR

T1 - Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6 = Phasengleichgewichte in binären systemen von Methanol mit Sulfolan, Tetraethylenglycoldimethylether und 18-krone-6 Kronenether

AU - Kuczynski, M.

AU - 't Hart, W.

AU - Westerterp, K.R.

PY - 1986

Y1 - 1986

N2 - The activity coefficients of methanol in sulfolane, tetraethylene glycol dimethyl ether (TEGDME) and 18-crown-6 under conditions of equilibrium have been determined in the temperature range 423–503 K and in the pressure range 0.28–3.5 MPa. A minimum in the activity coefficient was found for the methanol—TEGDME and methanol—18-crown-6 solutions.

AB - The activity coefficients of methanol in sulfolane, tetraethylene glycol dimethyl ether (TEGDME) and 18-crown-6 under conditions of equilibrium have been determined in the temperature range 423–503 K and in the pressure range 0.28–3.5 MPa. A minimum in the activity coefficient was found for the methanol—TEGDME and methanol—18-crown-6 solutions.

KW - IR-69633

U2 - 10.1016/0255-2701(86)85008-5

DO - 10.1016/0255-2701(86)85008-5

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VL - 20

SP - 53

EP - 58

JO - Chemical engineering and processing : process intensification

JF - Chemical engineering and processing : process intensification

SN - 0255-2701

IS - 1

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Kuczynski M, 't Hart W, Westerterp KR. Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6 = Phasengleichgewichte in binären systemen von Methanol mit Sulfolan, Tetraethylenglycoldimethylether und 18-krone-6 Kronenether. Chemical engineering and processing : process intensification. 1986;20(1):53-58. https://doi.org/10.1016/0255-2701(86)85008-5