Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Benzene (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0008 |
| 298.15 | 0.1206 | 0.0007 |
| 298.15 | 0.2642 | 0.0007 |
| 298.15 | 0.3982 | 0.0007 |
| 298.15 | 0.4644 | 0.0007 |
| 298.15 | 0.5321 | 0.0007 |
| 298.15 | 0.6074 | 0.0007 |
| 298.15 | 0.7069 | 0.0007 |
| 298.15 | 0.8131 | 0.0006 |
| 298.15 | 0.9162 | 0.0006 |
| 298.15 | 1.0000 | 0.0006 |
| 303.15 | 0.0000 | 0.0007 |
| 303.15 | 0.1206 | 0.0007 |
| 303.15 | 0.2642 | 0.0007 |
| 303.15 | 0.3982 | 0.0007 |
| 303.15 | 0.4644 | 0.0007 |
| 303.15 | 0.5321 | 0.0006 |
| 303.15 | 0.6074 | 0.0006 |
| 303.15 | 0.7069 | 0.0006 |
| 303.15 | 0.8131 | 0.0006 |
| 303.15 | 0.9162 | 0.0006 |
| 303.15 | 1.0000 | 0.0006 |
| 308.15 | 0.0000 | 0.0007 |
| 308.15 | 0.1206 | 0.0007 |
| 308.15 | 0.2642 | 0.0006 |
| 308.15 | 0.3982 | 0.0006 |
| 308.15 | 0.4644 | 0.0006 |
| 308.15 | 0.5321 | 0.0006 |
| 308.15 | 0.6074 | 0.0006 |
| 308.15 | 0.7069 | 0.0006 |
| 308.15 | 0.8131 | 0.0006 |
| 308.15 | 0.9162 | 0.0005 |
| 308.15 | 1.0000 | 0.0005 |
| 313.15 | 0.0000 | 0.0006 |
| 313.15 | 0.1206 | 0.0006 |
| 313.15 | 0.2642 | 0.0006 |
| 313.15 | 0.3982 | 0.0006 |
| 313.15 | 0.4644 | 0.0006 |
| 313.15 | 0.5321 | 0.0006 |
| 313.15 | 0.6074 | 0.0006 |
| 313.15 | 0.7069 | 0.0005 |
| 313.15 | 0.8131 | 0.0005 |
| 313.15 | 0.9162 | 0.0005 |
| 313.15 | 1.0000 | 0.0005 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Benzene (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0008 |
| 298.15 | 0.1206 | 0.0007 |
| 298.15 | 0.2642 | 0.0007 |
| 298.15 | 0.3982 | 0.0007 |
| 298.15 | 0.4644 | 0.0007 |
| 298.15 | 0.5321 | 0.0007 |
| 298.15 | 0.6074 | 0.0007 |
| 298.15 | 0.7069 | 0.0007 |
| 298.15 | 0.8131 | 0.0006 |
| 298.15 | 0.9162 | 0.0006 |
| 298.15 | 1.0000 | 0.0006 |
| 303.15 | 0.0000 | 0.0007 |
| 303.15 | 0.1206 | 0.0007 |
| 303.15 | 0.2642 | 0.0007 |
| 303.15 | 0.3982 | 0.0007 |
| 303.15 | 0.4644 | 0.0007 |
| 303.15 | 0.5321 | 0.0006 |
| 303.15 | 0.6074 | 0.0006 |
| 303.15 | 0.7069 | 0.0006 |
| 303.15 | 0.8131 | 0.0006 |
| 303.15 | 0.9162 | 0.0006 |
| 303.15 | 1.0000 | 0.0006 |
| 308.15 | 0.0000 | 0.0007 |
| 308.15 | 0.1206 | 0.0007 |
| 308.15 | 0.2642 | 0.0006 |
| 308.15 | 0.3982 | 0.0006 |
| 308.15 | 0.4644 | 0.0006 |
| 308.15 | 0.5321 | 0.0006 |
| 308.15 | 0.6074 | 0.0006 |
| 308.15 | 0.7069 | 0.0006 |
| 308.15 | 0.8131 | 0.0006 |
| 308.15 | 0.9162 | 0.0005 |
| 308.15 | 1.0000 | 0.0005 |
| 313.15 | 0.0000 | 0.0006 |
| 313.15 | 0.1206 | 0.0006 |
| 313.15 | 0.2642 | 0.0006 |
| 313.15 | 0.3982 | 0.0006 |
| 313.15 | 0.4644 | 0.0006 |
| 313.15 | 0.5321 | 0.0006 |
| 313.15 | 0.6074 | 0.0006 |
| 313.15 | 0.7069 | 0.0005 |
| 313.15 | 0.8131 | 0.0005 |
| 313.15 | 0.9162 | 0.0005 |
| 313.15 | 1.0000 | 0.0005 |
Operational conditions:
| Mole fraction of Benzene, chloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0804 | -0.0021 |
| 0.1272 | -0.0028 |
| 0.1794 | -0.0039 |
| 0.2258 | -0.0046 |
| 0.3043 | -0.0051 |
| 0.3684 | -0.0055 |
| 0.3962 | -0.0058 |
| 0.4666 | -0.0057 |
| 0.5384 | -0.0054 |
| 0.5675 | -0.0055 |
| 0.6363 | -0.0049 |
| 0.6999 | -0.0042 |
| 0.7777 | -0.0036 |
| 0.8235 | -0.0031 |
| 0.8974 | -0.0017 |
Operational conditions:
| Mole fraction of Benzene, chloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0804 | -0.0021 |
| 0.1272 | -0.0028 |
| 0.1794 | -0.0039 |
| 0.2258 | -0.0046 |
| 0.3043 | -0.0051 |
| 0.3684 | -0.0055 |
| 0.3962 | -0.0058 |
| 0.4666 | -0.0057 |
| 0.5384 | -0.0054 |
| 0.5675 | -0.0055 |
| 0.6363 | -0.0049 |
| 0.6999 | -0.0042 |
| 0.7777 | -0.0036 |
| 0.8235 | -0.0031 |
| 0.8974 | -0.0017 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Benzene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 1100.9 |
| 298.15 | 0.1206 | 1076.5 |
| 298.15 | 0.2642 | 1046.5 |
| 298.15 | 0.3982 | 1017.5 |
| 298.15 | 0.4644 | 1002.8 |
| 298.15 | 0.5321 | 987.7 |
| 298.15 | 0.6074 | 970.4 |
| 298.15 | 0.7069 | 946.8 |
| 298.15 | 0.8131 | 920.9 |
| 298.15 | 0.9162 | 895.0 |
| 298.15 | 1.0000 | 873.4 |
| 303.15 | 0.0000 | 1095.8 |
| 303.15 | 0.1206 | 1071.4 |
| 303.15 | 0.2642 | 1041.4 |
| 303.15 | 0.3982 | 1012.4 |
| 303.15 | 0.4644 | 997.7 |
| 303.15 | 0.5321 | 982.5 |
| 303.15 | 0.6074 | 965.2 |
| 303.15 | 0.7069 | 941.6 |
| 303.15 | 0.8131 | 915.7 |
| 303.15 | 0.9162 | 889.8 |
| 303.15 | 1.0000 | 868.2 |
| 308.15 | 0.0000 | 1090.8 |
| 308.15 | 0.1206 | 1066.4 |
| 308.15 | 0.2642 | 1036.3 |
| 308.15 | 0.3982 | 1007.3 |
| 308.15 | 0.4644 | 992.6 |
| 308.15 | 0.5321 | 977.3 |
| 308.15 | 0.6074 | 960.0 |
| 308.15 | 0.7069 | 936.4 |
| 308.15 | 0.8131 | 910.5 |
| 308.15 | 0.9162 | 884.6 |
| 308.15 | 1.0000 | 862.9 |
| 313.15 | 0.0000 | 1085.1 |
| 313.15 | 0.1206 | 1060.7 |
| 313.15 | 0.2642 | 1030.7 |
| 313.15 | 0.3982 | 1001.7 |
| 313.15 | 0.4644 | 987.0 |
| 313.15 | 0.5321 | 971.7 |
| 313.15 | 0.6074 | 954.5 |
| 313.15 | 0.7069 | 930.9 |
| 313.15 | 0.8131 | 905.0 |
| 313.15 | 0.9162 | 879.2 |
| 313.15 | 1.0000 | 857.4 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Benzene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 1100.9 |
| 298.15 | 0.1206 | 1076.5 |
| 298.15 | 0.2642 | 1046.5 |
| 298.15 | 0.3982 | 1017.5 |
| 298.15 | 0.4644 | 1002.8 |
| 298.15 | 0.5321 | 987.7 |
| 298.15 | 0.6074 | 970.4 |
| 298.15 | 0.7069 | 946.8 |
| 298.15 | 0.8131 | 920.9 |
| 298.15 | 0.9162 | 895.0 |
| 298.15 | 1.0000 | 873.4 |
| 303.15 | 0.0000 | 1095.8 |
| 303.15 | 0.1206 | 1071.4 |
| 303.15 | 0.2642 | 1041.4 |
| 303.15 | 0.3982 | 1012.4 |
| 303.15 | 0.4644 | 997.7 |
| 303.15 | 0.5321 | 982.5 |
| 303.15 | 0.6074 | 965.2 |
| 303.15 | 0.7069 | 941.6 |
| 303.15 | 0.8131 | 915.7 |
| 303.15 | 0.9162 | 889.8 |
| 303.15 | 1.0000 | 868.2 |
| 308.15 | 0.0000 | 1090.8 |
| 308.15 | 0.1206 | 1066.4 |
| 308.15 | 0.2642 | 1036.3 |
| 308.15 | 0.3982 | 1007.3 |
| 308.15 | 0.4644 | 992.6 |
| 308.15 | 0.5321 | 977.3 |
| 308.15 | 0.6074 | 960.0 |
| 308.15 | 0.7069 | 936.4 |
| 308.15 | 0.8131 | 910.5 |
| 308.15 | 0.9162 | 884.6 |
| 308.15 | 1.0000 | 862.9 |
| 313.15 | 0.0000 | 1085.1 |
| 313.15 | 0.1206 | 1060.7 |
| 313.15 | 0.2642 | 1030.7 |
| 313.15 | 0.3982 | 1001.7 |
| 313.15 | 0.4644 | 987.0 |
| 313.15 | 0.5321 | 971.7 |
| 313.15 | 0.6074 | 954.5 |
| 313.15 | 0.7069 | 930.9 |
| 313.15 | 0.8131 | 905.0 |
| 313.15 | 0.9162 | 879.2 |
| 313.15 | 1.0000 | 857.4 |