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Received December 13, 2002
Accepted June 4, 2003
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Vapor-Liquid Equilibria for 1,1,1-Trifluoro-2-(2,2,2-trifluoroethoxy)ethane +2-Methyl-2-propanol and Pentane+1,1,2,2-tetrafluoro-1-(2,2,2-trifluoroethoxy)ethane System

Department of Applied Molecular Chemistry, Nihon University, 1-2-1 Izumi-cho, Narashino, Chiba 275-8575, Japan 1Research Center, Asahi Glass Co., Ltd., 1150 Hazawa-cho, Kanagawa-ku, Yokohama 221-8755, Japan 2National Institute of Advanced Industrial Science and Technology (AIST), Research Center for Developing FluorinatedGreenhouse Gas Alternatives, Tsukuba Central 5-2 1-1-1 Higashi, Tsukuba, Ibaraki 305-8565, Japan
hiaki@dic.cit.nihon-u.ac.jp
Korean Journal of Chemical Engineering, September 2003, 20(5), 902-905(4), 10.1007/BF02697296
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Abstract

Isobaric vapor-liquid equilibrium (VLE) for two binary systems of 1,1,1-Trifluoro-2-(2,2,2-trifluoroethoxy) ethane+2-methyl-2-propanol and pentane+1,1,2,2-tetrafluoro-1-(2,2,2-trifluoroethoxy)ethane system have been measured at 101.3 kPa. The measurements were made in an equilibrium still, developed in a previous study, with circulation of both the vapor and liquid phases. The binary isobaric systems exhibit minimum boiling azeotropes. The thermodynamic consistencies of the experimental data were good by the Van Ness et al. and Herington methods. The experimental data for the binary systems investigated were correlated with activity coefficient equations. The nonrandom two-liquid_x000D_ (NRTL) equation yielded a good correlation of activity coefficients.

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