Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of Methyl Alcohol (2) - Liquid | Mole fraction of Methyl Alcohol (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0240 | 0.0830 |
0.0370 | 0.1260 |
0.0540 | 0.1780 |
0.0740 | 0.2320 |
0.1000 | 0.2980 |
0.1150 | 0.3350 |
0.1400 | 0.3890 |
0.1620 | 0.4310 |
0.1870 | 0.4760 |
0.2080 | 0.5120 |
0.2480 | 0.5700 |
0.3020 | 0.6400 |
0.3300 | 0.6710 |
0.3660 | 0.7060 |
0.3970 | 0.7350 |
0.4500 | 0.7780 |
0.5070 | 0.8170 |
0.6060 | 0.8720 |
0.6470 | 0.8950 |
0.7030 | 0.9150 |
0.7620 | 0.9360 |
0.8100 | 0.9520 |
0.8670 | 0.9680 |
0.8860 | 0.9730 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of Methyl Alcohol (2) - Liquid | Mole fraction of Methyl Alcohol (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0240 | 0.0830 |
0.0370 | 0.1260 |
0.0540 | 0.1780 |
0.0740 | 0.2320 |
0.1000 | 0.2980 |
0.1150 | 0.3350 |
0.1400 | 0.3890 |
0.1620 | 0.4310 |
0.1870 | 0.4760 |
0.2080 | 0.5120 |
0.2480 | 0.5700 |
0.3020 | 0.6400 |
0.3300 | 0.6710 |
0.3660 | 0.7060 |
0.3970 | 0.7350 |
0.4500 | 0.7780 |
0.5070 | 0.8170 |
0.6060 | 0.8720 |
0.6470 | 0.8950 |
0.7030 | 0.9150 |
0.7620 | 0.9360 |
0.8100 | 0.9520 |
0.8670 | 0.9680 |
0.8860 | 0.9730 |
1.0000 | 1.0000 |
Operational conditions:
Mole fraction of Amylene hydrate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0908 | -0.2563 |
0.1814 | -0.5223 |
0.2731 | -0.8036 |
0.3644 | -1.0447 |
0.4608 | -1.2 |
0.5513 | -1.268 |
0.6416 | -1.2156 |
0.7319 | -1.0696 |
0.8195 | -0.7997 |
0.9101 | -0.4219 |
Operational conditions:
Mole fraction of Amylene hydrate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0908 | -0.2563 |
0.1814 | -0.5223 |
0.2731 | -0.8036 |
0.3644 | -1.0447 |
0.4608 | -1.2 |
0.5513 | -1.268 |
0.6416 | -1.2156 |
0.7319 | -1.0696 |
0.8195 | -0.7997 |
0.9101 | -0.4219 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of Methyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 375.14 |
0.0240 | 373.42 |
0.0370 | 372.50 |
0.0540 | 371.32 |
0.0740 | 370.05 |
0.1000 | 368.45 |
0.1150 | 367.50 |
0.1400 | 366.05 |
0.1620 | 364.85 |
0.1870 | 363.54 |
0.2080 | 362.44 |
0.2480 | 360.52 |
0.3020 | 358.05 |
0.3300 | 356.85 |
0.3660 | 355.42 |
0.3970 | 354.20 |
0.4500 | 352.25 |
0.5070 | 350.25 |
0.6060 | 347.25 |
0.6470 | 346.05 |
0.7030 | 344.52 |
0.7620 | 343.02 |
0.8100 | 341.84 |
0.8670 | 340.52 |
0.8860 | 340.10 |
1.0000 | 337.68 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of Methyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 375.14 |
0.0240 | 373.42 |
0.0370 | 372.50 |
0.0540 | 371.32 |
0.0740 | 370.05 |
0.1000 | 368.45 |
0.1150 | 367.50 |
0.1400 | 366.05 |
0.1620 | 364.85 |
0.1870 | 363.54 |
0.2080 | 362.44 |
0.2480 | 360.52 |
0.3020 | 358.05 |
0.3300 | 356.85 |
0.3660 | 355.42 |
0.3970 | 354.20 |
0.4500 | 352.25 |
0.5070 | 350.25 |
0.6060 | 347.25 |
0.6470 | 346.05 |
0.7030 | 344.52 |
0.7620 | 343.02 |
0.8100 | 341.84 |
0.8670 | 340.52 |
0.8860 | 340.10 |
1.0000 | 337.68 |