2 0 2009 ker ati 1 journal Original Kerboub, W.[Wahiba] Atik, Z.[Zadjia] J. Chem. Thermodyn. 2009 2009-04-07 Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation 2,2,2-Trifluoroethanol Type (II) phase diagram Tie line Correlation NRTL UNIQUAC 10.1016/j.jct.2008.10.017 41 549-552 1 hexane C6H14 1 Commercial source 1 99.5 3 Gas chromatography 2 Molecular sieve treatment 2 heptane C7H16 1 Commercial source 1 99.5 3 Gas chromatography 2 Molecular sieve treatment 3 methanol CH4O 1 Commercial source 1 99.7 3 Gas chromatography 2 Molecular sieve treatment 4 2-propanol C3H8O 1 Commercial source 1 99.5 3 Gas chromatography 2 Molecular sieve treatment 5 2,2,2-trifluoroethanol C2H3F3O 1 Commercial source 1 99.2 3 Gas chromatography 2 Molecular sieve treatment 1 1 Principal objective of the work WZ TRC 2/10/2009 1 Mass density, kg/m3 Vibrating tube method Liquid Direct value, X Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 298.15 5 1 654.8 4 2 1 Principal objective of the work WZ TRC 2/10/2009 1 Mass density, kg/m3 Vibrating tube method Liquid Direct value, X Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 298.15 5 1 680 4 3 1 Principal objective of the work WZ TRC 2/10/2009 1 Mass density, kg/m3 Vibrating tube method Liquid Direct value, X Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 298.15 5 1 787 4 4 1 Principal objective of the work WZ TRC 2/10/2009 1 Mass density, kg/m3 Vibrating tube method Liquid Direct value, X Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 298.15 5 1 781.4 4 5 1 Principal objective of the work WZ TRC 2/10/2009 1 Mass density, kg/m3 Vibrating tube method Liquid Direct value, X Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 298.15 5 1 1382.4 5 3 1 5 1 1 1 Principal objective of the work JWM TRC 4/3/2009 1 Mole fraction Chromatography 1 Liquid mixture 1 Direct value, X 1 Author 2 Mole fraction Chromatography 3 Liquid mixture 2 Direct value, X 1 Author 3 Mole fraction Chromatography 1 Liquid mixture 2 Direct value, X 1 Author Liquid mixture 1 Liquid mixture 2 Pressure, kPa 100 3 1 Temperature, K 1 Author 2 Mole fraction 3 Liquid mixture 1 1 Author 1 288.15 5 1 .03 2 .172 3 1 .0003 1 .828 3 1 .0003 2 .845 3 1 .0003 3 .155 3 1 .0003 1 288.15 5 1 .03 2 0 0 1 .0003 1 .829 3 1 .0003 2 0 0 1 .0003 3 .099 2 1 .0003 1 288.15 5 1 .03 2 .019 2 1 .0003 1 .82 3 1 .0003 2 .092 2 1 .0003 3 .087 2 1 .0003 1 288.15 5 1 .03 2 .027 2 1 .0003 1 .831 3 1 .0003 2 .154 3 1 .0003 3 .08 2 1 .0003 1 288.15 5 1 .03 2 .039 2 1 .0003 1 .827 3 1 .0003 2 .188 3 1 .0003 3 .082 2 1 .0003 1 288.15 5 1 .03 2 .078 2 1 .0003 1 .822 3 1 .0003 2 .264 3 1 .0003 3 .102 3 1 .0003 1 288.15 5 1 .03 2 .098 2 1 .0003 1 .813 3 1 .0003 2 .321 3 1 .0003 3 .093 2 1 .0003 1 288.15 5 1 .03 2 .118 3 1 .0003 1 .81 3 1 .0003 2 .377 3 1 .0003 3 .104 3 1 .0003 1 288.15 5 1 .03 2 .142 3 1 .0003 1 .808 3 1 .0003 2 .465 3 1 .0003 3 .093 2 1 .0003 1 288.15 5 1 .03 2 .147 3 1 .0003 1 .808 3 1 .0003 2 .554 3 1 .0003 3 .096 2 1 .0003 1 288.15 5 1 .03 2 .156 3 1 .0003 1 .81 3 1 .0003 2 .62 3 1 .0003 3 .098 2 1 .0003 1 288.15 5 1 .03 2 .166 3 1 .0003 1 .806 3 1 .0003 2 .723 3 1 .0003 3 .114 3 1 .0003 1 298.15 5 1 .03 2 .259 3 1 .0003 1 .741 3 1 .0003 2 .786 3 1 .0003 3 .214 3 1 .0003 1 298.15 5 1 .03 2 0 0 1 .0003 1 .761 3 1 .0003 2 0 0 1 .0003 3 .155 3 1 .0003 1 298.15 5 1 .03 2 .032 2 1 .0003 1 .757 3 1 .0003 2 .084 2 1 .0003 3 .146 3 1 .0003 1 298.15 5 1 .03 2 .066 2 1 .0003 1 .755 3 1 .0003 2 .16 3 1 .0003 3 .151 3 1 .0003 1 298.15 5 1 .03 2 .111 3 1 .0003 1 .751 3 1 .0003 2 .231 3 1 .0003 3 .162 3 1 .0003 1 298.15 5 1 .03 2 .13 3 1 .0003 1 .742 3 1 .0003 2 .302 3 1 .0003 3 .16 3 1 .0003 1 298.15 5 1 .03 2 .142 3 1 .0003 1 .741 3 1 .0003 2 .358 3 1 .0003 3 .154 3 1 .0003 1 298.15 5 1 .03 2 .155 3 1 .0003 1 .751 3 1 .0003 2 .417 3 1 .0003 3 .165 3 1 .0003 1 298.15 5 1 .03 2 .183 3 1 .0003 1 .746 3 1 .0003 2 .501 3 1 .0003 3 .164 3 1 .0003 1 298.15 5 1 .03 2 .22 3 1 .0003 1 .742 3 1 .0003 2 .596 3 1 .0003 3 .161 3 1 .0003 1 298.15 5 1 .03 2 .226 3 1 .0003 1 .744 3 1 .0003 2 .696 3 1 .0003 3 .174 3 1 .0003 1 298.15 5 1 .03 2 .241 3 1 .0003 1 .742 3 1 .0003 2 .742 3 1 .0003 3 .19 3 1 .0003 1 303.15 5 1 .03 2 .324 3 1 .0003 1 .676 3 1 .0003 2 .724 3 1 .0003 3 .276 3 1 .0003 1 303.15 5 1 .03 2 0 0 1 .0003 1 .726 3 1 .0003 2 0 0 1 .0003 3 .184 3 1 .0003 1 303.15 5 1 .03 2 .04 2 1 .0003 1 .71 3 1 .0003 2 .086 2 1 .0003 3 .21 3 1 .0003 1 303.15 5 1 .03 2 .057 2 1 .0003 1 .697 3 1 .0003 2 .125 3 1 .0003 3 .218 3 1 .0003 1 303.15 5 1 .03 2 .088 2 1 .0003 1 .691 3 1 .0003 2 .192 3 1 .0003 3 .217 3 1 .0003 1 303.15 5 1 .03 2 .121 3 1 .0003 1 .679 3 1 .0003 2 .238 3 1 .0003 3 .207 3 1 .0003 1 303.15 5 1 .03 2 .155 3 1 .0003 1 .668 3 1 .0003 2 .327 3 1 .0003 3 .213 3 1 .0003 1 303.15 5 1 .03 2 .182 3 1 .0003 1 .667 3 1 .0003 2 .371 3 1 .0003 3 .222 3 1 .0003 1 303.15 5 1 .03 2 .22 3 1 .0003 1 .661 3 1 .0003 2 .431 3 1 .0003 3 .23 3 1 .0003 1 303.15 5 1 .03 2 .233 3 1 .0003 1 .661 3 1 .0003 2 .486 3 1 .0003 3 .231 3 1 .0003 1 303.15 5 1 .03 2 .263 3 1 .0003 1 .658 3 1 .0003 2 .541 3 1 .0003 3 .24 3 1 .0003 1 303.15 5 1 .03 2 .293 3 1 .0003 1 .657 3 1 .0003 2 .634 3 1 .0003 3 .257 3 1 .0003