Operational condition: Temperature, K = 313.15 (Liquid)
Mole fraction of 1-Pentanol (1) - Liquid | Mole fraction of 1-Pentanol (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.0491 | 0.0143 |
0.1037 | 0.0172 |
0.1492 | 0.0183 |
0.1989 | 0.0195 |
0.2492 | 0.0210 |
0.2993 | 0.0225 |
0.3493 | 0.0240 |
0.3991 | 0.0255 |
0.4010 | 0.0256 |
0.4494 | 0.0272 |
0.4511 | 0.0272 |
0.4993 | 0.0290 |
0.5012 | 0.0290 |
0.5492 | 0.0311 |
0.5514 | 0.0312 |
0.5993 | 0.0339 |
0.6016 | 0.0341 |
0.6517 | 0.0378 |
0.7025 | 0.0428 |
0.7517 | 0.0495 |
0.8019 | 0.0594 |
0.8516 | 0.0753 |
0.9015 | 0.1063 |
0.9512 | 0.1918 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Pentanol (1) - Liquid | Mole fraction of 1-Pentanol (1) - Gas |
---|---|
0.0059 | 0.0057 |
0.0095 | 0.0083 |
0.0106 | 0.0090 |
0.0157 | 0.0125 |
0.0222 | 0.0155 |
0.0272 | 0.0184 |
0.0335 | 0.0204 |
0.0436 | 0.0238 |
0.0457 | 0.0239 |
0.0496 | 0.0250 |
0.0554 | 0.0268 |
0.0654 | 0.0284 |
0.0680 | 0.0292 |
Operational condition: Temperature, K = 313.15 (Liquid)
Mole fraction of 1-Pentanol (1) - Liquid | Mole fraction of 1-Pentanol (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.0491 | 0.0143 |
0.1037 | 0.0172 |
0.1492 | 0.0183 |
0.1989 | 0.0195 |
0.2492 | 0.0210 |
0.2993 | 0.0225 |
0.3493 | 0.0240 |
0.3991 | 0.0255 |
0.4010 | 0.0256 |
0.4494 | 0.0272 |
0.4511 | 0.0272 |
0.4993 | 0.0290 |
0.5012 | 0.0290 |
0.5492 | 0.0311 |
0.5514 | 0.0312 |
0.5993 | 0.0339 |
0.6016 | 0.0341 |
0.6517 | 0.0378 |
0.7025 | 0.0428 |
0.7517 | 0.0495 |
0.8019 | 0.0594 |
0.8516 | 0.0753 |
0.9015 | 0.1063 |
0.9512 | 0.1918 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Pentanol (1) - Liquid | Mole fraction of 1-Pentanol (1) - Gas |
---|---|
0.0059 | 0.0057 |
0.0095 | 0.0083 |
0.0106 | 0.0090 |
0.0157 | 0.0125 |
0.0222 | 0.0155 |
0.0272 | 0.0184 |
0.0335 | 0.0204 |
0.0436 | 0.0238 |
0.0457 | 0.0239 |
0.0496 | 0.0250 |
0.0554 | 0.0268 |
0.0654 | 0.0284 |
0.0680 | 0.0292 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Pentanol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0000 | 0.0000 |
298.15 | 0.0500 | 0.3333 |
298.15 | 0.1001 | 0.4401 |
298.15 | 0.1501 | 0.5205 |
298.15 | 0.2022 | 0.5810 |
298.15 | 0.2522 | 0.6220 |
298.15 | 0.3022 | 0.6487 |
298.15 | 0.3523 | 0.6609 |
298.15 | 0.4023 | 0.6584 |
298.15 | 0.4523 | 0.6414 |
298.15 | 0.5022 | 0.6092 |
298.15 | 0.5522 | 0.5735 |
298.15 | 0.6022 | 0.5274 |
298.15 | 0.6522 | 0.4711 |
298.15 | 0.7022 | 0.4110 |
298.15 | 0.7522 | 0.3472 |
298.15 | 0.8021 | 0.2719 |
298.15 | 0.8501 | 0.2061 |
298.15 | 0.9000 | 0.1381 |
298.15 | 0.9500 | 0.0677 |
298.15 | 1.0000 | 0.0000 |
313.15 | 0.0000 | 0.0000 |
313.15 | 0.0500 | 0.4490 |
313.15 | 0.1000 | 0.5819 |
313.15 | 0.1501 | 0.6733 |
313.15 | 0.2021 | 0.7393 |
313.15 | 0.2522 | 0.7853 |
313.15 | 0.3022 | 0.8094 |
313.15 | 0.3521 | 0.8187 |
313.15 | 0.4022 | 0.8099 |
313.15 | 0.4522 | 0.7835 |
313.15 | 0.5022 | 0.7459 |
313.15 | 0.5522 | 0.7095 |
313.15 | 0.6022 | 0.6342 |
313.15 | 0.6519 | 0.5831 |
313.15 | 0.7019 | 0.4941 |
313.15 | 0.7521 | 0.4121 |
313.15 | 0.8021 | 0.3345 |
313.15 | 0.8501 | 0.2502 |
313.15 | 0.9000 | 0.1596 |
313.15 | 0.9500 | 0.0798 |
313.15 | 1.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Pentanol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0000 | 0.0000 |
298.15 | 0.0500 | 0.3333 |
298.15 | 0.1001 | 0.4401 |
298.15 | 0.1501 | 0.5205 |
298.15 | 0.2022 | 0.5810 |
298.15 | 0.2522 | 0.6220 |
298.15 | 0.3022 | 0.6487 |
298.15 | 0.3523 | 0.6609 |
298.15 | 0.4023 | 0.6584 |
298.15 | 0.4523 | 0.6414 |
298.15 | 0.5022 | 0.6092 |
298.15 | 0.5522 | 0.5735 |
298.15 | 0.6022 | 0.5274 |
298.15 | 0.6522 | 0.4711 |
298.15 | 0.7022 | 0.4110 |
298.15 | 0.7522 | 0.3472 |
298.15 | 0.8021 | 0.2719 |
298.15 | 0.8501 | 0.2061 |
298.15 | 0.9000 | 0.1381 |
298.15 | 0.9500 | 0.0677 |
298.15 | 1.0000 | 0.0000 |
313.15 | 0.0000 | 0.0000 |
313.15 | 0.0500 | 0.4490 |
313.15 | 0.1000 | 0.5819 |
313.15 | 0.1501 | 0.6733 |
313.15 | 0.2021 | 0.7393 |
313.15 | 0.2522 | 0.7853 |
313.15 | 0.3022 | 0.8094 |
313.15 | 0.3521 | 0.8187 |
313.15 | 0.4022 | 0.8099 |
313.15 | 0.4522 | 0.7835 |
313.15 | 0.5022 | 0.7459 |
313.15 | 0.5522 | 0.7095 |
313.15 | 0.6022 | 0.6342 |
313.15 | 0.6519 | 0.5831 |
313.15 | 0.7019 | 0.4941 |
313.15 | 0.7521 | 0.4121 |
313.15 | 0.8021 | 0.3345 |
313.15 | 0.8501 | 0.2502 |
313.15 | 0.9000 | 0.1596 |
313.15 | 0.9500 | 0.0798 |
313.15 | 1.0000 | 0.0000 |
Operational conditions:
Mole fraction of Cyclohexane (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 810.8 |
0.0810 | 807.1 |
0.1607 | 803.6 |
0.2403 | 800.1 |
0.3487 | 795.4 |
0.4396 | 791.7 |
0.5597 | 787.0 |
0.6498 | 783.7 |
0.7408 | 780.6 |
0.8499 | 777.1 |
0.9406 | 774.8 |
1.0000 | 773.6 |
Operational conditions:
Mole fraction of Cyclohexane (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 810.8 |
0.0810 | 807.1 |
0.1607 | 803.6 |
0.2403 | 800.1 |
0.3487 | 795.4 |
0.4396 | 791.7 |
0.5597 | 787.0 |
0.6498 | 783.7 |
0.7408 | 780.6 |
0.8499 | 777.1 |
0.9406 | 774.8 |
1.0000 | 773.6 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Pentanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0059 | 353.80 |
0.0095 | 353.90 |
0.0106 | 353.90 |
0.0157 | 354.00 |
0.0222 | 354.10 |
0.0272 | 354.30 |
0.0335 | 354.40 |
0.0436 | 354.30 |
0.0457 | 354.50 |
0.0496 | 354.40 |
0.0554 | 354.60 |
0.0654 | 354.70 |
0.0680 | 354.70 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Pentanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0059 | 353.80 |
0.0095 | 353.90 |
0.0106 | 353.90 |
0.0157 | 354.00 |
0.0222 | 354.10 |
0.0272 | 354.30 |
0.0335 | 354.40 |
0.0436 | 354.30 |
0.0457 | 354.50 |
0.0496 | 354.40 |
0.0554 | 354.60 |
0.0654 | 354.70 |
0.0680 | 354.70 |
Operational condition: Temperature, K = 313.15 (Liquid)
Mole fraction of 1-Pentanol (1) - Liquid | Vapor or sublimation pressure, kPa - Gas |
---|---|
0.0000 | 24.57 |
0.0491 | 24.33 |
0.1037 | 24.07 |
0.1492 | 23.79 |
0.1989 | 23.48 |
0.2492 | 23.14 |
0.2993 | 22.76 |
0.3493 | 22.33 |
0.3991 | 21.85 |
0.4010 | 21.83 |
0.4494 | 21.28 |
0.4511 | 21.27 |
0.4993 | 20.61 |
0.5012 | 20.61 |
0.5492 | 19.83 |
0.5514 | 19.93 |
0.5993 | 18.88 |
0.6016 | 18.86 |
0.6517 | 17.72 |
0.7025 | 16.32 |
0.7517 | 14.71 |
0.8019 | 12.75 |
0.8516 | 10.46 |
0.9015 | 7.75 |
0.9512 | 4.56 |
1.0000 | 0.90 |
Operational condition: Temperature, K = 313.15 (Liquid)
Mole fraction of 1-Pentanol (1) - Liquid | Vapor or sublimation pressure, kPa - Gas |
---|---|
0.0000 | 24.57 |
0.0491 | 24.33 |
0.1037 | 24.07 |
0.1492 | 23.79 |
0.1989 | 23.48 |
0.2492 | 23.14 |
0.2993 | 22.76 |
0.3493 | 22.33 |
0.3991 | 21.85 |
0.4010 | 21.83 |
0.4494 | 21.28 |
0.4511 | 21.27 |
0.4993 | 20.61 |
0.5012 | 20.61 |
0.5492 | 19.83 |
0.5514 | 19.93 |
0.5993 | 18.88 |
0.6016 | 18.86 |
0.6517 | 17.72 |
0.7025 | 16.32 |
0.7517 | 14.71 |
0.8019 | 12.75 |
0.8516 | 10.46 |
0.9015 | 7.75 |
0.9512 | 4.56 |
1.0000 | 0.90 |