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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received June 13, 2009
Accepted July 21, 2009
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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High pressure isothermal vapor-liquid equilibria of carbon dioxide+1,1-difluoroethane

Department of Chemical and Biomolecular Engineering, Sogang University, 1142, Seoul 121-742, Korea
limjs@sogang.ac.kr
Korean Journal of Chemical Engineering, January 2010, 27(1), 261-266(6), 10.1007/s11814-009-0334-0
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Abstract

Vapor-liquid equilibrium data for the binary mixture of carbon dioxide (CO2)+1,1-difluoroethane (HFC-152a) were measured at five evenly spaced temperatures of (273.15, 283.15, 293.15, 303.15 and 313.15) K by using a circulation-type equilibrium apparatus in which both vapor and liquid phases were recirculated. The experimental data were correlated with the Peng-Robinson equation of state (PR-EoS) using the Wong-Sandler mixing rules combined with the NRTL excess Gibbs free energy model and the Carnahan-Starling-DeSantis equation of state (CSD EoS). Almost all the calculated values with these two models showed good agreement with the experimental data.

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