Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0545 | -0.0837 |
0.1711 | -0.2508 |
0.2234 | -0.3211 |
0.2761 | -0.3887 |
0.3509 | -0.4777 |
0.4214 | -0.5513 |
0.5512 | -0.6468 |
0.5879 | -0.6606 |
0.6213 | -0.6666 |
0.6821 | -0.6589 |
0.7511 | -0.6149 |
0.8145 | -0.5344 |
0.8914 | -0.3735 |
0.9413 | -0.2254 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0545 | -0.0837 |
0.1711 | -0.2508 |
0.2234 | -0.3211 |
0.2761 | -0.3887 |
0.3509 | -0.4777 |
0.4214 | -0.5513 |
0.5512 | -0.6468 |
0.5879 | -0.6606 |
0.6213 | -0.6666 |
0.6821 | -0.6589 |
0.7511 | -0.6149 |
0.8145 | -0.5344 |
0.8914 | -0.3735 |
0.9413 | -0.2254 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of Aniline (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.0000 | 13.79 |
0.0502 | 12.83 |
0.1501 | 11.52 |
0.2510 | 9.87 |
0.3511 | 8.16 |
0.4504 | 6.60 |
0.5503 | 5.07 |
0.6513 | 3.76 |
0.7522 | 2.44 |
0.8511 | 1.39 |
0.9502 | 0.56 |
1.0000 | 0.12 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of Aniline (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.0000 | 13.79 |
0.0502 | 12.83 |
0.1501 | 11.52 |
0.2510 | 9.87 |
0.3511 | 8.16 |
0.4504 | 6.60 |
0.5503 | 5.07 |
0.6513 | 3.76 |
0.7522 | 2.44 |
0.8511 | 1.39 |
0.9502 | 0.56 |
1.0000 | 0.12 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0912 | 1564.0 |
0.1516 | 1543.0 |
0.2414 | 1510.0 |
0.2990 | 1490.0 |
0.3541 | 1470.0 |
0.4417 | 1438.0 |
0.5312 | 1404.0 |
0.5943 | 1379.0 |
0.6511 | 1357.0 |
0.7344 | 1324.0 |
0.8117 | 1294.0 |
0.8830 | 1267.0 |
0.9413 | 1245.0 |
0.9812 | 1231.0 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0912 | 1564.0 |
0.1516 | 1543.0 |
0.2414 | 1510.0 |
0.2990 | 1490.0 |
0.3541 | 1470.0 |
0.4417 | 1438.0 |
0.5312 | 1404.0 |
0.5943 | 1379.0 |
0.6511 | 1357.0 |
0.7344 | 1324.0 |
0.8117 | 1294.0 |
0.8830 | 1267.0 |
0.9413 | 1245.0 |
0.9812 | 1231.0 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0702 | -9.7000e-08 |
0.1767 | -2.4500e-07 |
0.2381 | -3.2200e-07 |
0.2952 | -3.8400e-07 |
0.3347 | -4.2000e-07 |
0.3913 | -4.5900e-07 |
0.4354 | -4.8000e-07 |
0.4904 | -4.9200e-07 |
0.5525 | -4.8700e-07 |
0.6280 | -4.5600e-07 |
0.6989 | -4.0100e-07 |
0.7412 | -3.5900e-07 |
0.8548 | -2.1500e-07 |
0.9204 | -1.1900e-07 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0702 | -9.7000e-08 |
0.1767 | -2.4500e-07 |
0.2381 | -3.2200e-07 |
0.2952 | -3.8400e-07 |
0.3347 | -4.2000e-07 |
0.3913 | -4.5900e-07 |
0.4354 | -4.8000e-07 |
0.4904 | -4.9200e-07 |
0.5525 | -4.8700e-07 |
0.6280 | -4.5600e-07 |
0.6989 | -4.0100e-07 |
0.7412 | -3.5900e-07 |
0.8548 | -2.1500e-07 |
0.9204 | -1.1900e-07 |