2 0 2009 gha gha 1 journal Original Ghanadzadeh, H. Ghanadzadeh, A. Bahrpaima, K.[Kh.] Fluid Phase Equilib. 2009 2009-04-01 Measurement and prediction of tie-line data for mixtures of (water + 1-propanol + diisopropyl ether): LLE diagrams as a function of temperature LLE Equilibrium diagrams 1-Propanol Diisopropyl ether UNIFAC model 10.1016/j.fluid.2008.11.014 277 126-130 1 water H2O 1 Commercial source 1 Fractional distillation 1 99.9 3 Estimation 2 1-propanol C3H8O 1 Commercial source 1 99.5 3 Stated by supplier 3 isopropyl ether C6H14O 1 Commercial source 1 99 2 Stated by supplier 2 1 Principal objective of the work PW TRC 3/5/2009 1 Mass density, kg/m3 Vibrating tube method Liquid Direct value, X 1 Author Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 Author 1 298.2 4 1 .1 1 799.62 5 1 .01 2 1 Principal objective of the work PW TRC 3/5/2009 1 Refractive index (Na D-line) Standard Abbe refractometry Liquid Direct value, X 1 Author Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 298.2 4 1 1.3835 5 1 .00013835 3 1 Principal objective of the work PW TRC 3/5/2009 1 Mass density, kg/m3 Vibrating tube method Liquid Direct value, X 1 Author Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 Author 1 298.2 4 1 .1 1 718.79 5 1 .01 3 1 Principal objective of the work PW TRC 3/5/2009 1 Refractive index (Na D-line) Standard Abbe refractometry Liquid Direct value, X 1 Author Liquid Pressure, kPa 101.325 6 1 Temperature, K 1 298.2 4 1 1.3653 5 1 .00013653 2 1 3 1 1 1 Principal objective of the work JWM TRC 3/31/2009 1 Mass fraction Chromatography 2 Liquid mixture 1 Direct value, X 2 Mole fraction Chromatography 1 Liquid mixture 2 Direct value, X 3 Mole fraction Chromatography 2 Liquid mixture 2 Direct value, X Liquid mixture 1 Liquid mixture 2 Pressure, kPa 101 3 1 Temperature, K 2 Mole fraction 1 Liquid mixture 1 1 298.2 4 2 .9984 4 1 0 0 2 .0016 2 3 0 0 1 298.2 4 2 .9288 4 1 .064 3 2 .005 2 3 .0889 3 1 298.2 4 2 .855 4 1 .128 4 2 .011 3 3 .1899 4 1 298.2 4 2 .825 4 1 .1521 4 2 .0175 3 3 .2528 4 1 298.2 4 2 .7591 4 1 .1992 4 2 .048 3 3 .3208 4 1 298.2 4 2 .6177 4 1 .2887 4 2 .075 3 3 .341 4 1 298.2 4 2 .5095 4 1 .3405 4 2 .0936 3 3 .351 4 1 308.2 4 2 .9979 4 1 0 0 2 .0278 3 3 0 0 1 308.2 4 2 .9726 4 1 .025 3 2 .058 3 3 .1026 4 1 308.2 4 2 .9476 4 1 .0495 3 2 .1106 4 3 .2003 4 1 308.2 4 2 .9193 4 1 .0778 3 2 .1591 4 3 .2648 4 1 308.2 4 2 .845 4 1 .1521 4 2 .2187 4 3 .3127 4 1 308.2 4 2 .788 4 1 .206 4 2 .264 4 3 .338 4 1 308.2 4 2 .7019 4 1 .271 4 2 .3318 4 3 .3614 4 1 313.2 4 2 .9962 4 1 0 0 2 .0338 3 3 0 0 1 313.2 4 2 .928 4 1 .0677 3 2 .0464 3 3 .0472 3 1 313.2 4 2 .8841 4 1 .1075 4 2 .0708 3 3 .1097 4 1 313.2 4 2 .8401 4 1 .145 4 2 .088 3 3 .144 4 1 313.2 4 2 .7901 4 1 .1872 4 2 .1252 4 3 .2065 4 1 313.2 4 2 .7324 4 1 .2288 4 2 .1465 4 3 .2381 4 1 313.2 4 2 .6307 4 1 .2987 4 2 .179 4 3 .2802 4 3 1 1 1 Principal objective of the work JWM TRC 3/31/2009 1 Mole fraction Chromatography 1 Liquid mixture 1 Direct value, X Liquid mixture 1 Liquid mixture 2 1 Temperature, K 2 Pressure, kPa 1 298.2 4 2 101 3 1 .9984 4 1 308.2 4 2 101 3 1 .9979 4 1 313.2 4 2 101 3 1 .9962 4 3 1 1 1 Principal objective of the work JWM TRC 3/31/2009 1 Mole fraction Chromatography 1 Liquid mixture 2 Direct value, X Liquid mixture 2 Liquid mixture 1 1 Temperature, K 2 Pressure, kPa 1 298.2 4 2 101 3 1 .0016 2 1 308.2 4 2 101 3 1 .0278 3 1 313.2 4 2 101 3 1 .0338 3