Operational conditions:
| Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0570 | -0.0140 |
| 0.1040 | -0.0300 |
| 0.2010 | -0.0610 |
| 0.2980 | -0.0830 |
| 0.3980 | -0.1010 |
| 0.4970 | -0.1090 |
| 0.5970 | -0.1060 |
| 0.6960 | -0.0950 |
| 0.7990 | -0.0770 |
| 0.9010 | -0.0440 |
| 0.9540 | -0.0230 |
Operational conditions:
| Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0570 | -0.0140 |
| 0.1040 | -0.0300 |
| 0.2010 | -0.0610 |
| 0.2980 | -0.0830 |
| 0.3980 | -0.1010 |
| 0.4970 | -0.1090 |
| 0.5970 | -0.1060 |
| 0.6960 | -0.0950 |
| 0.7990 | -0.0770 |
| 0.9010 | -0.0440 |
| 0.9540 | -0.0230 |
Operational conditions:
| Mole fraction of Propane, 2-chloro-2-methyl- (1) - Liquid | Kinematic viscosity, m2/s - Liquid |
|---|---|
| 0.0000 | 5.5930e-07 |
| 0.0481 | 5.5860e-07 |
| 0.0972 | 5.5750e-07 |
| 0.1960 | 5.5540e-07 |
| 0.2907 | 5.5450e-07 |
| 0.3874 | 5.5390e-07 |
| 0.4878 | 5.5430e-07 |
| 0.5888 | 5.5540e-07 |
| 0.7000 | 5.5710e-07 |
| 0.7912 | 5.5900e-07 |
| 0.8945 | 5.6150e-07 |
| 0.9474 | 5.6340e-07 |
| 1.0000 | 5.6560e-07 |
Operational conditions:
| Mole fraction of Propane, 2-chloro-2-methyl- (1) - Liquid | Kinematic viscosity, m2/s - Liquid |
|---|---|
| 0.0000 | 5.5930e-07 |
| 0.0481 | 5.5860e-07 |
| 0.0972 | 5.5750e-07 |
| 0.1960 | 5.5540e-07 |
| 0.2907 | 5.5450e-07 |
| 0.3874 | 5.5390e-07 |
| 0.4878 | 5.5430e-07 |
| 0.5888 | 5.5540e-07 |
| 0.7000 | 5.5710e-07 |
| 0.7912 | 5.5900e-07 |
| 0.8945 | 5.6150e-07 |
| 0.9474 | 5.6340e-07 |
| 1.0000 | 5.6560e-07 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0505 | 837.22 |
| 298.15 | 0.1080 | 838.65 |
| 298.15 | 0.2065 | 840.58 |
| 298.15 | 0.3136 | 842.3 |
| 298.15 | 0.4125 | 843.81 |
| 298.15 | 0.5156 | 845.26 |
| 298.15 | 0.6124 | 846.46 |
| 298.15 | 0.7107 | 847.59 |
| 298.15 | 0.8031 | 848.42 |
| 298.15 | 0.9022 | 848.98 |
| 298.15 | 0.9476 | 849.12 |
| 313.15 | 0.0517 | 819.88 |
| 313.15 | 0.0895 | 820.9 |
| 313.15 | 0.1950 | 823.23 |
| 313.15 | 0.3015 | 825.36 |
| 313.15 | 0.3969 | 827.1 |
| 313.15 | 0.4986 | 828.77 |
| 313.15 | 0.6050 | 830.31 |
| 313.15 | 0.6978 | 831.4 |
| 313.15 | 0.7998 | 832.45 |
| 313.15 | 0.8947 | 833.18 |
| 313.15 | 0.9490 | 833.54 |
Operational conditions:
| Mole fraction of Propane, 2-chloro-2-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 849.28 |
| 0.0481 | 849.09 |
| 0.0972 | 848.97 |
| 0.1960 | 848.4 |
| 0.2907 | 847.61 |
| 0.3874 | 846.54 |
| 0.4878 | 845.21 |
| 0.5888 | 843.72 |
| 0.7000 | 842.04 |
| 0.7912 | 840.61 |
| 0.8945 | 838.65 |
| 0.9474 | 837.24 |
| 1.0000 | 835.75 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0505 | 837.22 |
| 298.15 | 0.1080 | 838.65 |
| 298.15 | 0.2065 | 840.58 |
| 298.15 | 0.3136 | 842.3 |
| 298.15 | 0.4125 | 843.81 |
| 298.15 | 0.5156 | 845.26 |
| 298.15 | 0.6124 | 846.46 |
| 298.15 | 0.7107 | 847.59 |
| 298.15 | 0.8031 | 848.42 |
| 298.15 | 0.9022 | 848.98 |
| 298.15 | 0.9476 | 849.12 |
| 313.15 | 0.0517 | 819.88 |
| 313.15 | 0.0895 | 820.9 |
| 313.15 | 0.1950 | 823.23 |
| 313.15 | 0.3015 | 825.36 |
| 313.15 | 0.3969 | 827.1 |
| 313.15 | 0.4986 | 828.77 |
| 313.15 | 0.6050 | 830.31 |
| 313.15 | 0.6978 | 831.4 |
| 313.15 | 0.7998 | 832.45 |
| 313.15 | 0.8947 | 833.18 |
| 313.15 | 0.9490 | 833.54 |
Operational conditions:
| Mole fraction of Propane, 2-chloro-2-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 849.28 |
| 0.0481 | 849.09 |
| 0.0972 | 848.97 |
| 0.1960 | 848.4 |
| 0.2907 | 847.61 |
| 0.3874 | 846.54 |
| 0.4878 | 845.21 |
| 0.5888 | 843.72 |
| 0.7000 | 842.04 |
| 0.7912 | 840.61 |
| 0.8945 | 838.65 |
| 0.9474 | 837.24 |
| 1.0000 | 835.75 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0505 | 993.8 |
| 298.15 | 0.1080 | 1006.1 |
| 298.15 | 0.2065 | 1027.5 |
| 298.15 | 0.3136 | 1050.9 |
| 298.15 | 0.4125 | 1072.6 |
| 298.15 | 0.5156 | 1095.2 |
| 298.15 | 0.6124 | 1116.5 |
| 298.15 | 0.7107 | 1138.2 |
| 298.15 | 0.8031 | 1158.7 |
| 298.15 | 0.9022 | 1180.6 |
| 298.15 | 0.9476 | 1190.7 |
| 313.15 | 0.0517 | 932.6 |
| 313.15 | 0.0895 | 941.2 |
| 313.15 | 0.1950 | 964.0 |
| 313.15 | 0.3015 | 986.5 |
| 313.15 | 0.3969 | 1006.8 |
| 313.15 | 0.4986 | 1028.7 |
| 313.15 | 0.6050 | 1051.5 |
| 313.15 | 0.6978 | 1071.1 |
| 313.15 | 0.7998 | 1092.0 |
| 313.15 | 0.8947 | 1111.7 |
| 313.15 | 0.9490 | 1123.7 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0505 | 993.8 |
| 298.15 | 0.1080 | 1006.1 |
| 298.15 | 0.2065 | 1027.5 |
| 298.15 | 0.3136 | 1050.9 |
| 298.15 | 0.4125 | 1072.6 |
| 298.15 | 0.5156 | 1095.2 |
| 298.15 | 0.6124 | 1116.5 |
| 298.15 | 0.7107 | 1138.2 |
| 298.15 | 0.8031 | 1158.7 |
| 298.15 | 0.9022 | 1180.6 |
| 298.15 | 0.9476 | 1190.7 |
| 313.15 | 0.0517 | 932.6 |
| 313.15 | 0.0895 | 941.2 |
| 313.15 | 0.1950 | 964.0 |
| 313.15 | 0.3015 | 986.5 |
| 313.15 | 0.3969 | 1006.8 |
| 313.15 | 0.4986 | 1028.7 |
| 313.15 | 0.6050 | 1051.5 |
| 313.15 | 0.6978 | 1071.1 |
| 313.15 | 0.7998 | 1092.0 |
| 313.15 | 0.8947 | 1111.7 |
| 313.15 | 0.9490 | 1123.7 |