2 0 2009 tam li 0 journal Original Tamura, K.[Kazuhiro] Li, X.[Xiaoli] Li, H.[Hengde] J. Chem. Thermodyn. 2009 2009-04-07 Temperature dependence on mutual solubility of binary (methanol + limonene) mixture and (liquid + liquid) equilibria of ternary (methanol + ethanol + limonene) mixture (Liquid + liquid) equilibria (LLE) Limonene Alcohol UNIQUAC model 10.1016/j.jct.2008.10.013 41 564-568 1 (R)-(+)-limonene C10H16 1 Commercial source 1 99 2 Stated by supplier 2 None used 2 methanol CH4O 1 Commercial source 1 99.7 3 Stated by supplier 2 None used 3 ethanol C2H6O 1 Commercial source 1 99.5 3 Stated by supplier 2 None used 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 1 837.31 5 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 1 786.62 5 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 1 785.24 5 2 1 1 1 Principal objective of the work WZ TRC 2/10/2009 1 Mole fraction Chromatography 2 Liquid mixture 1 Direct value, X Liquid mixture 1 Liquid mixture 2 Pressure, kPa 101 3 1 Temperature, K 1 288.15 5 1 .9062 4 1 293.3 5 1 .8957 4 1 298.15 5 1 .8819 4 1 302.94 5 1 .8626 4 1 308.15 5 1 .8381 4 1 312.14 5 1 .8115 4 1 313.37 5 1 .7889 4 2 1 1 1 Principal objective of the work WZ TRC 2/10/2009 1 Mole fraction Chromatography 2 Liquid mixture 2 Direct value, X Liquid mixture 2 Liquid mixture 1 Pressure, kPa 101 3 1 Temperature, K 1 288.15 5 1 .2076 4 1 293.3 5 1 .2317 4 1 298.15 5 1 .2769 4 1 302.94 5 1 .3128 4 1 308.15 5 1 .3839 4 1 312.14 5 1 .4712 4 1 313.37 5 1 .5473 4 3 1 2 1 1 1 Principal objective of the work JWM TRC 4/3/2009 1 Mole fraction Chromatography 3 Liquid mixture 2 Direct value, X 2 Mole fraction Chromatography 2 Liquid mixture 1 Direct value, X 3 Mole fraction Chromatography 3 Liquid mixture 1 Direct value, X Liquid mixture 2 Liquid mixture 1 Pressure, kPa 101 3 1 Temperature, K 2 Mole fraction 2 Liquid mixture 2 1 288.15 5 2 .2256 4 1 .0152 3 2 .8452 4 3 .0422 3 1 288.15 5 2 .2484 4 1 .0318 3 2 .7784 4 3 .0882 3 1 288.15 5 2 .2705 4 1 .0557 3 2 .7176 4 3 .1239 4 1 288.15 5 2 .372 4 1 .0841 3 2 .6271 4 3 .1333 4 1 288.15 5 2 .4002 4 1 .101 4 2 .5923 4 3 .1403 4 1 298.15 5 2 .2715 4 1 .0082 2 2 .8534 4 3 .0271 3 1 298.15 5 2 .2844 4 1 .0168 3 2 .8261 4 3 .0429 3 1 298.15 5 2 .3422 4 1 .0362 3 2 .748 4 3 .0728 3 1 298.15 5 2 .4508 4 1 .0758 3 2 .6301 4 3 .1097 4 1 308.15 5 2 .4105 4 1 .0053 2 2 .8182 4 3 .0099 2 1 308.15 5 2 .433 4 1 .0132 3 2 .784 4 3 .0217 3 1 308.15 5 2 .4524 4 1 .0157 3 2 .7741 4 3 .0234 3 1 308.15 5 2 .4719 4 1 .0235 3 2 .756 4 3 .0247 3