Operational conditions:
Mole fraction of Propane, 1,3-dichloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0493 | -0.0311 |
0.0986 | -0.0616 |
0.1536 | -0.0997 |
0.2082 | -0.1392 |
0.2610 | -0.1784 |
0.3126 | -0.2176 |
0.3627 | -0.2551 |
0.4084 | -0.2763 |
0.4405 | -0.2915 |
0.4492 | -0.2958 |
0.5044 | -0.3034 |
0.5692 | -0.3032 |
0.6438 | -0.2875 |
0.7284 | -0.2480 |
0.8181 | -0.1835 |
0.9124 | -0.1029 |
Operational conditions:
Mole fraction of Propane, 1,3-dichloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0493 | -0.0311 |
0.0986 | -0.0616 |
0.1536 | -0.0997 |
0.2082 | -0.1392 |
0.2610 | -0.1784 |
0.3126 | -0.2176 |
0.3627 | -0.2551 |
0.4084 | -0.2763 |
0.4405 | -0.2915 |
0.4492 | -0.2958 |
0.5044 | -0.3034 |
0.5692 | -0.3032 |
0.6438 | -0.2875 |
0.7284 | -0.2480 |
0.8181 | -0.1835 |
0.9124 | -0.1029 |
Operational conditions:
Mole fraction of Pentanoic acid, ethyl ester (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0395 | 1159.55 |
0.0785 | 1141.75 |
0.1207 | 1123.43 |
0.1642 | 1105.29 |
0.2098 | 1087.19 |
0.2576 | 1069.12 |
0.3081 | 1050.97 |
0.3623 | 1032.41 |
0.4179 | 1014.41 |
0.4804 | 995.25 |
0.5380 | 978.58 |
0.6036 | 960.5 |
0.7440 | 925.06 |
0.8249 | 906.38 |
0.9085 | 888.3 |
Operational conditions:
Mole fraction of Pentanoic acid, ethyl ester (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0395 | 1159.55 |
0.0785 | 1141.75 |
0.1207 | 1123.43 |
0.1642 | 1105.29 |
0.2098 | 1087.19 |
0.2576 | 1069.12 |
0.3081 | 1050.97 |
0.3623 | 1032.41 |
0.4179 | 1014.41 |
0.4804 | 995.25 |
0.5380 | 978.58 |
0.6036 | 960.5 |
0.7440 | 925.06 |
0.8249 | 906.38 |
0.9085 | 888.3 |