Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0856 | -0.1104 |
0.1321 | -0.1702 |
0.1976 | -0.2512 |
0.2434 | -0.3043 |
0.3122 | -0.3760 |
0.3876 | -0.4403 |
0.4444 | -0.4766 |
0.4878 | -0.4962 |
0.5548 | -0.5110 |
0.6233 | -0.5048 |
0.6921 | -0.4747 |
0.7432 | -0.4356 |
0.8767 | -0.2612 |
0.9549 | -0.1072 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0856 | -0.1104 |
0.1321 | -0.1702 |
0.1976 | -0.2512 |
0.2434 | -0.3043 |
0.3122 | -0.3760 |
0.3876 | -0.4403 |
0.4444 | -0.4766 |
0.4878 | -0.4962 |
0.5548 | -0.5110 |
0.6233 | -0.5048 |
0.6921 | -0.4747 |
0.7432 | -0.4356 |
0.8767 | -0.2612 |
0.9549 | -0.1072 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of Aniline, N-methyl- (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.0000 | 13.79 |
0.0511 | 12.96 |
0.1510 | 11.24 |
0.2522 | 9.48 |
0.3501 | 7.67 |
0.4531 | 6.15 |
0.5521 | 4.73 |
0.6501 | 3.39 |
0.7533 | 2.15 |
0.8502 | 1.11 |
0.9521 | 0.41 |
1.0000 | 0.11 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of Aniline, N-methyl- (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.0000 | 13.79 |
0.0511 | 12.96 |
0.1510 | 11.24 |
0.2522 | 9.48 |
0.3501 | 7.67 |
0.4531 | 6.15 |
0.5521 | 4.73 |
0.6501 | 3.39 |
0.7533 | 2.15 |
0.8502 | 1.11 |
0.9521 | 0.41 |
1.0000 | 0.11 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0541 | 1509.0 |
0.1321 | 1490.0 |
0.2316 | 1468.0 |
0.2811 | 1457.0 |
0.3612 | 1437.0 |
0.4112 | 1424.0 |
0.4932 | 1400.0 |
0.5638 | 1377.0 |
0.6148 | 1360.0 |
0.6919 | 1332.0 |
0.7418 | 1313.0 |
0.8141 | 1287.0 |
0.8992 | 1257.0 |
0.9514 | 1239.0 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0541 | 1509.0 |
0.1321 | 1490.0 |
0.2316 | 1468.0 |
0.2811 | 1457.0 |
0.3612 | 1437.0 |
0.4112 | 1424.0 |
0.4932 | 1400.0 |
0.5638 | 1377.0 |
0.6148 | 1360.0 |
0.6919 | 1332.0 |
0.7418 | 1313.0 |
0.8141 | 1287.0 |
0.8992 | 1257.0 |
0.9514 | 1239.0 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0764 | -7.2000e-08 |
0.1416 | -1.2500e-07 |
0.1921 | -1.5900e-07 |
0.2440 | -1.8900e-07 |
0.2905 | -2.1000e-07 |
0.3451 | -2.2700e-07 |
0.3984 | -2.3700e-07 |
0.4515 | -2.4000e-07 |
0.5224 | -2.3400e-07 |
0.6130 | -2.1000e-07 |
0.6873 | -1.7800e-07 |
0.7531 | -1.4400e-07 |
0.8231 | -1.0300e-07 |
0.9191 | -4.5000e-08 |
Operational conditions:
Mole fraction of Tetrahydropyran (2) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0764 | -7.2000e-08 |
0.1416 | -1.2500e-07 |
0.1921 | -1.5900e-07 |
0.2440 | -1.8900e-07 |
0.2905 | -2.1000e-07 |
0.3451 | -2.2700e-07 |
0.3984 | -2.3700e-07 |
0.4515 | -2.4000e-07 |
0.5224 | -2.3400e-07 |
0.6130 | -2.1000e-07 |
0.6873 | -1.7800e-07 |
0.7531 | -1.4400e-07 |
0.8231 | -1.0300e-07 |
0.9191 | -4.5000e-08 |