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 |
---|---|
0.0613 | -0.1616 |
0.1622 | -0.4135 |
0.2241 | -0.5476 |
0.2774 | -0.6508 |
0.3503 | -0.7685 |
0.4231 | -0.8484 |
0.5511 | -0.9003 |
0.5812 | -0.8962 |
0.6223 | -0.8733 |
0.6816 | -0.8171 |
0.7519 | -0.7151 |
0.8127 | -0.5867 |
0.8928 | -0.3713 |
0.9514 | -0.1822 |
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 |
---|---|
0.0613 | -0.1616 |
0.1622 | -0.4135 |
0.2241 | -0.5476 |
0.2774 | -0.6508 |
0.3503 | -0.7685 |
0.4231 | -0.8484 |
0.5511 | -0.9003 |
0.5812 | -0.8962 |
0.6223 | -0.8733 |
0.6816 | -0.8171 |
0.7519 | -0.7151 |
0.8127 | -0.5867 |
0.8928 | -0.3713 |
0.9514 | -0.1822 |
Operational conditions:
Mole fraction of 1,3-Dioxolane (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0812 | 1587.0 |
0.1413 | 1576.0 |
0.2212 | 1557.0 |
0.2916 | 1539.0 |
0.3488 | 1523.0 |
0.4621 | 1489.0 |
0.5219 | 1470.0 |
0.5928 | 1447.0 |
0.6414 | 1431.0 |
0.7131 | 1406.0 |
0.8001 | 1374.0 |
0.8715 | 1347.0 |
0.9213 | 1327.0 |
0.9711 | 1307.0 |
Operational conditions:
Mole fraction of 1,3-Dioxolane (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0812 | 1587.0 |
0.1413 | 1576.0 |
0.2212 | 1557.0 |
0.2916 | 1539.0 |
0.3488 | 1523.0 |
0.4621 | 1489.0 |
0.5219 | 1470.0 |
0.5928 | 1447.0 |
0.6414 | 1431.0 |
0.7131 | 1406.0 |
0.8001 | 1374.0 |
0.8715 | 1347.0 |
0.9213 | 1327.0 |
0.9711 | 1307.0 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of Aniline (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
---|---|
0.0000 | 21.50 |
0.1324 | 17.37 |
0.2421 | 14.52 |
0.3453 | 11.27 |
0.4443 | 8.72 |
0.5216 | 7.23 |
0.6211 | 5.31 |
0.7435 | 3.36 |
0.8435 | 1.63 |
0.9041 | 0.93 |
1.0000 | 0.12 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of Aniline (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
---|---|
0.0000 | 21.50 |
0.1324 | 17.37 |
0.2421 | 14.52 |
0.3453 | 11.27 |
0.4443 | 8.72 |
0.5216 | 7.23 |
0.6211 | 5.31 |
0.7435 | 3.36 |
0.8435 | 1.63 |
0.9041 | 0.93 |
1.0000 | 0.12 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of 1,3-Dioxolane (1) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0789 | -1.3400e-07 |
0.1132 | -1.8800e-07 |
0.2204 | -3.3000e-07 |
0.3111 | -4.2800e-07 |
0.4281 | -4.9700e-07 |
0.4916 | -5.1600e-07 |
0.5230 | -5.1700e-07 |
0.5999 | -4.9300e-07 |
0.6342 | -4.7700e-07 |
0.7114 | -4.1800e-07 |
0.8202 | -2.9400e-07 |
0.8913 | -1.9000e-07 |
0.9233 | -1.3800e-07 |
0.9718 | -5.2500e-08 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of 1,3-Dioxolane (1) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0789 | -1.3400e-07 |
0.1132 | -1.8800e-07 |
0.2204 | -3.3000e-07 |
0.3111 | -4.2800e-07 |
0.4281 | -4.9700e-07 |
0.4916 | -5.1600e-07 |
0.5230 | -5.1700e-07 |
0.5999 | -4.9300e-07 |
0.6342 | -4.7700e-07 |
0.7114 | -4.1800e-07 |
0.8202 | -2.9400e-07 |
0.8913 | -1.9000e-07 |
0.9233 | -1.3800e-07 |
0.9718 | -5.2500e-08 |