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 |
---|---|
0.0853 | -0.3823 |
0.1423 | -0.5433 |
0.2533 | -0.6782 |
0.3765 | -0.6524 |
0.4531 | -0.5904 |
0.5123 | -0.5316 |
0.5976 | -0.4402 |
0.6432 | -0.3877 |
0.7123 | -0.3134 |
0.7943 | -0.2348 |
0.8543 | -0.1713 |
0.8912 | -0.1345 |
0.9321 | -0.0932 |
0.9721 | -0.0374 |
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 |
---|---|
0.0853 | -0.3823 |
0.1423 | -0.5433 |
0.2533 | -0.6782 |
0.3765 | -0.6524 |
0.4531 | -0.5904 |
0.5123 | -0.5316 |
0.5976 | -0.4402 |
0.6432 | -0.3877 |
0.7123 | -0.3134 |
0.7943 | -0.2348 |
0.8543 | -0.1713 |
0.8912 | -0.1345 |
0.9321 | -0.0932 |
0.9721 | -0.0374 |
Operational conditions:
Mole fraction of 1,3-Dioxolane (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0415 | 1521.0 |
0.1211 | 1511.0 |
0.2001 | 1501.0 |
0.2754 | 1490.0 |
0.3512 | 1477.0 |
0.4222 | 1463.0 |
0.4943 | 1447.0 |
0.5421 | 1436.0 |
0.6213 | 1415.0 |
0.7003 | 1393.0 |
0.7832 | 1367.0 |
0.8632 | 1341.0 |
0.9011 | 1329.0 |
0.9632 | 1307.0 |
Operational conditions:
Mole fraction of 1,3-Dioxolane (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0415 | 1521.0 |
0.1211 | 1511.0 |
0.2001 | 1501.0 |
0.2754 | 1490.0 |
0.3512 | 1477.0 |
0.4222 | 1463.0 |
0.4943 | 1447.0 |
0.5421 | 1436.0 |
0.6213 | 1415.0 |
0.7003 | 1393.0 |
0.7832 | 1367.0 |
0.8632 | 1341.0 |
0.9011 | 1329.0 |
0.9632 | 1307.0 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of Aniline, N-methyl- (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
---|---|
0.0000 | 21.50 |
0.1123 | 17.44 |
0.2222 | 14.91 |
0.3343 | 12.15 |
0.4543 | 8.95 |
0.5256 | 7.23 |
0.6543 | 4.59 |
0.7543 | 2.56 |
0.8432 | 1.15 |
0.9001 | 1.05 |
1.0000 | 0.07 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of Aniline, N-methyl- (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
---|---|
0.0000 | 21.50 |
0.1123 | 17.44 |
0.2222 | 14.91 |
0.3343 | 12.15 |
0.4543 | 8.95 |
0.5256 | 7.23 |
0.6543 | 4.59 |
0.7543 | 2.56 |
0.8432 | 1.15 |
0.9001 | 1.05 |
1.0000 | 0.07 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of 1,3-Dioxolane (1) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0709 | -1.8000e-08 |
0.1771 | -4.5000e-08 |
0.2387 | -6.3000e-08 |
0.2958 | -8.0000e-08 |
0.3349 | -8.8000e-08 |
0.3916 | -9.5000e-08 |
0.4361 | -1.0200e-07 |
0.4912 | -1.1000e-07 |
0.5531 | -1.1200e-07 |
0.6272 | -1.0400e-07 |
0.6992 | -9.3000e-08 |
0.7417 | -8.8000e-08 |
0.8545 | -5.1000e-08 |
0.9213 | -3.0000e-08 |
Operational condition: Temperature, K = 308.15 (Liquid)
Mole fraction of 1,3-Dioxolane (1) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0709 | -1.8000e-08 |
0.1771 | -4.5000e-08 |
0.2387 | -6.3000e-08 |
0.2958 | -8.0000e-08 |
0.3349 | -8.8000e-08 |
0.3916 | -9.5000e-08 |
0.4361 | -1.0200e-07 |
0.4912 | -1.1000e-07 |
0.5531 | -1.1200e-07 |
0.6272 | -1.0400e-07 |
0.6992 | -9.3000e-08 |
0.7417 | -8.8000e-08 |
0.8545 | -5.1000e-08 |
0.9213 | -3.0000e-08 |