Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of 1,3-Dioxolane (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0754 | -0.2205 |
0.1632 | -0.4640 |
0.2424 | -0.6468 |
0.3213 | -0.7861 |
0.4001 | -0.8728 |
0.4843 | -0.9061 |
0.5655 | -0.8712 |
0.6112 | -0.8266 |
0.6979 | -0.6962 |
0.7432 | -0.6087 |
0.8080 | -0.4667 |
0.8831 | -0.2811 |
0.9311 | -0.1633 |
0.9621 | -0.0868 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of 1,3-Dioxolane (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0754 | -0.2205 |
0.1632 | -0.4640 |
0.2424 | -0.6468 |
0.3213 | -0.7861 |
0.4001 | -0.8728 |
0.4843 | -0.9061 |
0.5655 | -0.8712 |
0.6112 | -0.8266 |
0.6979 | -0.6962 |
0.7432 | -0.6087 |
0.8080 | -0.4667 |
0.8831 | -0.2811 |
0.9311 | -0.1633 |
0.9621 | -0.0868 |
Operational conditions:
Mole fraction of 1,3-Dioxolane (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.1122 | 1539.0 |
0.1891 | 1526.0 |
0.2413 | 1516.0 |
0.2911 | 1506.0 |
0.3212 | 1500.0 |
0.4011 | 1484.0 |
0.4513 | 1473.0 |
0.5651 | 1444.0 |
0.6637 | 1415.0 |
0.6989 | 1404.0 |
0.7512 | 1386.0 |
0.8319 | 1358.0 |
0.9071 | 1330.0 |
0.9713 | 1306.0 |
Operational conditions:
Mole fraction of 1,3-Dioxolane (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.1122 | 1539.0 |
0.1891 | 1526.0 |
0.2413 | 1516.0 |
0.2911 | 1506.0 |
0.3212 | 1500.0 |
0.4011 | 1484.0 |
0.4513 | 1473.0 |
0.5651 | 1444.0 |
0.6637 | 1415.0 |
0.6989 | 1404.0 |
0.7512 | 1386.0 |
0.8319 | 1358.0 |
0.9071 | 1330.0 |
0.9713 | 1306.0 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of o-Toluidine (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
---|---|
0.0000 | 21.50 |
0.1532 | 18.51 |
0.2432 | 15.01 |
0.3553 | 12.16 |
0.4432 | 9.89 |
0.5556 | 8.03 |
0.6671 | 6.19 |
0.7432 | 4.27 |
0.8654 | 2.27 |
0.9010 | 1.08 |
1.0000 | 0.11 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of o-Toluidine (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
---|---|
0.0000 | 21.50 |
0.1532 | 18.51 |
0.2432 | 15.01 |
0.3553 | 12.16 |
0.4432 | 9.89 |
0.5556 | 8.03 |
0.6671 | 6.19 |
0.7432 | 4.27 |
0.8654 | 2.27 |
0.9010 | 1.08 |
1.0000 | 0.11 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of 1,3-Dioxolane (1) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0549 | -8.4000e-08 |
0.1721 | -2.5100e-07 |
0.2239 | -3.1200e-07 |
0.2769 | -3.7500e-07 |
0.3510 | -4.4300e-07 |
0.4217 | -4.8600e-07 |
0.5518 | -5.1200e-07 |
0.5889 | -5.1200e-07 |
0.6218 | -4.9700e-07 |
0.6831 | -4.6600e-07 |
0.7523 | -4.0700e-07 |
0.8147 | -3.2800e-07 |
0.8916 | -2.1600e-07 |
0.9407 | -1.2300e-07 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of 1,3-Dioxolane (1) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0549 | -8.4000e-08 |
0.1721 | -2.5100e-07 |
0.2239 | -3.1200e-07 |
0.2769 | -3.7500e-07 |
0.3510 | -4.4300e-07 |
0.4217 | -4.8600e-07 |
0.5518 | -5.1200e-07 |
0.5889 | -5.1200e-07 |
0.6218 | -4.9700e-07 |
0.6831 | -4.6600e-07 |
0.7523 | -4.0700e-07 |
0.8147 | -3.2800e-07 |
0.8916 | -2.1600e-07 |
0.9407 | -1.2300e-07 |