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Vapor-liquid Phase Equilibria for CO_2+Tertpentanol Binary System at Elevated Pressures
Authors:WANG Lin  LUO Jian-cheng  YANG Hao  CHEN Kai-xun Chemistry  Pharmaceutical Engineering College  Nanyang Normal University  Nanyang  PRChina  Chemical Engineering College  Northwest University  Xi'an  Chemical Engineering College  Nanyang Institute of Technology  Nanyang
Institution:WANG Lin1,2,LUO Jian-cheng3,YANG Hao1 and CHEN Kai-xun2 1.Chemistry and Pharmaceutical Engineering College,Nanyang Normal University,Nanyang 473061,P.R.China,2.Chemical Engineering College,Northwest University,Xi'an 710069,3.Chemical Engineering College,Nanyang Institute of Technology,Nanyang 473004
Abstract:Vapor-liquid phase equilibrium data of tertpentanol in carbon dioxide were measured at temperatures of 313.4,323.4,333.5 and 343.5 K and in the pressure range of 4.56 11.44MPa.The phase equilibium apparatus used in the work was a variable-volume high-pressure cell.The experimental data were reasonably correlated with Peng-Robinson equation of state(PR-EOS) together with van der Waals-2 two-parameter mixing rules.Henry's Law constants and partial molar volumes of CO2 at infinite dilution were estimated with ...
Keywords:Carbon dioxide  Tertpentanol  Phase equilibrium  Henry's Law constant  Partial molar volume  
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