Operational conditions:
Mole fraction of Butane, 1,4-dichloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0443 | -0.0154 |
0.0938 | -0.0412 |
0.1472 | -0.0653 |
0.2021 | -0.0957 |
0.2576 | -0.1328 |
0.3103 | -0.1673 |
0.3615 | -0.2059 |
0.4093 | -0.2313 |
0.4542 | -0.2540 |
0.4637 | -0.2596 |
0.5038 | -0.2688 |
0.5509 | -0.2731 |
0.6143 | -0.2673 |
0.6866 | -0.2475 |
0.7631 | -0.2110 |
0.8429 | -0.1558 |
0.9262 | -0.0846 |
Operational conditions:
Mole fraction of Butane, 1,4-dichloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0443 | -0.0154 |
0.0938 | -0.0412 |
0.1472 | -0.0653 |
0.2021 | -0.0957 |
0.2576 | -0.1328 |
0.3103 | -0.1673 |
0.3615 | -0.2059 |
0.4093 | -0.2313 |
0.4542 | -0.2540 |
0.4637 | -0.2596 |
0.5038 | -0.2688 |
0.5509 | -0.2731 |
0.6143 | -0.2673 |
0.6866 | -0.2475 |
0.7631 | -0.2110 |
0.8429 | -0.1558 |
0.9262 | -0.0846 |
Operational conditions:
Mole fraction of Pentanoic acid, ethyl ester (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0426 | 1118.97 |
0.0881 | 1103.57 |
0.1345 | 1088.34 |
0.1844 | 1072.46 |
0.2407 | 1055.13 |
0.2932 | 1039.54 |
0.3462 | 1024.28 |
0.4021 | 1008.72 |
0.4541 | 994.67 |
0.5187 | 977.83 |
0.5829 | 961.7 |
0.6452 | 946.59 |
0.7045 | 932.66 |
0.7796 | 915.67 |
0.8521 | 899.89 |
0.9250 | 884.57 |
Operational conditions:
Mole fraction of Pentanoic acid, ethyl ester (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0426 | 1118.97 |
0.0881 | 1103.57 |
0.1345 | 1088.34 |
0.1844 | 1072.46 |
0.2407 | 1055.13 |
0.2932 | 1039.54 |
0.3462 | 1024.28 |
0.4021 | 1008.72 |
0.4541 | 994.67 |
0.5187 | 977.83 |
0.5829 | 961.7 |
0.6452 | 946.59 |
0.7045 | 932.66 |
0.7796 | 915.67 |
0.8521 | 899.89 |
0.9250 | 884.57 |