Mixture of n-Hexane + 1-Pentanol

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n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

1-Pentanol

Name
1-Pentanol
InChI
InChI=1S/C5H12O/c1-2-3-4-5-6/h6H,2-5H2,1H3
InChI Key
AMQJEAYHLZJPGS-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCCCO
Mol. Weight (g/mol)
88.15
CAS
71-41-0
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (4)
  3. Tboil - Boiling temperature at pressure P, K (2)
  4. Vapor or sublimation pressure, kPa (2)

Mole fraction of 1-Pentanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of 1-Pentanol (2) - Liquid Mole fraction of 1-Pentanol (2) - Gas
0.0106 0.0072
0.0207 0.0102
0.0278 0.0130
0.0288 0.0131
0.0354 0.0142
0.0395 0.0150
0.0467 0.0159
0.0518 0.0172
0.0657 0.0193
0.0694 0.0197
0.0835 0.0204
0.0904 0.0209
0.0958 0.0214

Mole fraction of 1-Pentanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of 1-Pentanol (2) - Liquid Mole fraction of 1-Pentanol (2) - Gas
0.0106 0.0072
0.0207 0.0102
0.0278 0.0130
0.0288 0.0131
0.0354 0.0142
0.0395 0.0150
0.0467 0.0159
0.0518 0.0172
0.0657 0.0193
0.0694 0.0197
0.0835 0.0204
0.0904 0.0209
0.0958 0.0214

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Pentanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0504 0.3293
298.15 0.0999 0.4132
298.15 0.1509 0.4656
298.15 0.2010 0.5013
298.15 0.2524 0.5269
298.15 0.3027 0.5336
298.15 0.3522 0.5378
298.15 0.4030 0.5242
298.15 0.4528 0.5058
298.15 0.5035 0.4776
298.15 0.5535 0.4416
298.15 0.6025 0.3971
298.15 0.6525 0.3463
298.15 0.7015 0.2901
298.15 0.7514 0.2356
298.15 0.8021 0.1788
298.15 0.8518 0.1266
298.15 0.9004 0.0696
298.15 0.9499 0.0210
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0504 0.4551
313.15 0.1000 0.5692
313.15 0.1510 0.6377
313.15 0.2011 0.6801
313.15 0.2525 0.7059
313.15 0.3007 0.7209
313.15 0.3503 0.7245
313.15 0.4032 0.7116
313.15 0.4530 0.6886
313.15 0.5039 0.6520
313.15 0.5539 0.6051
313.15 0.6027 0.5473
313.15 0.6527 0.4874
313.15 0.7016 0.4154
313.15 0.7515 0.3401
313.15 0.8019 0.2648
313.15 0.8517 0.2000
313.15 0.9004 0.1282
313.15 0.9499 0.0674
313.15 1.0000 0.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of 1-Pentanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0241 0.2870
0.0501 0.3550
0.1085 0.4310
0.1504 0.4700
0.1912 0.5060
0.2341 0.5300
0.2905 0.5380
0.3433 0.5430
0.3934 0.5360
0.4452 0.5230
0.5771 0.4110
0.5794 0.4120
0.6531 0.3340
0.6979 0.2810
0.7463 0.2240
0.8030 0.1540
0.0573 0.3710
0.9021 0.0630

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Pentanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0504 0.3293
298.15 0.0999 0.4132
298.15 0.1509 0.4656
298.15 0.2010 0.5013
298.15 0.2524 0.5269
298.15 0.3027 0.5336
298.15 0.3522 0.5378
298.15 0.4030 0.5242
298.15 0.4528 0.5058
298.15 0.5035 0.4776
298.15 0.5535 0.4416
298.15 0.6025 0.3971
298.15 0.6525 0.3463
298.15 0.7015 0.2901
298.15 0.7514 0.2356
298.15 0.8021 0.1788
298.15 0.8518 0.1266
298.15 0.9004 0.0696
298.15 0.9499 0.0210
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0504 0.4551
313.15 0.1000 0.5692
313.15 0.1510 0.6377
313.15 0.2011 0.6801
313.15 0.2525 0.7059
313.15 0.3007 0.7209
313.15 0.3503 0.7245
313.15 0.4032 0.7116
313.15 0.4530 0.6886
313.15 0.5039 0.6520
313.15 0.5539 0.6051
313.15 0.6027 0.5473
313.15 0.6527 0.4874
313.15 0.7016 0.4154
313.15 0.7515 0.3401
313.15 0.8019 0.2648
313.15 0.8517 0.2000
313.15 0.9004 0.1282
313.15 0.9499 0.0674
313.15 1.0000 0.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of 1-Pentanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0241 0.2870
0.0501 0.3550
0.1085 0.4310
0.1504 0.4700
0.1912 0.5060
0.2341 0.5300
0.2905 0.5380
0.3433 0.5430
0.3934 0.5360
0.4452 0.5230
0.5771 0.4110
0.5794 0.4120
0.6531 0.3340
0.6979 0.2810
0.7463 0.2240
0.8030 0.1540
0.0573 0.3710
0.9021 0.0630

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0106 341.90
0.0207 342.00
0.0278 342.40
0.0288 342.40
0.0354 342.20
0.0395 342.40
0.0467 342.50
0.0518 342.40
0.0657 342.60
0.0694 342.90
0.0835 342.70
0.0904 342.70
0.0958 342.70

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0106 341.90
0.0207 342.00
0.0278 342.40
0.0288 342.40
0.0354 342.20
0.0395 342.40
0.0467 342.50
0.0518 342.40
0.0657 342.60
0.0694 342.90
0.0835 342.70
0.0904 342.70
0.0958 342.70

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 1-Pentanol (2) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 37.19
0.0287 36.63
0.0813 36.21
0.1338 35.77
0.1857 35.31
0.2380 34.81
0.2899 34.27
0.3416 33.69
0.3931 33.04
0.4013 33.04
0.4445 32.30
0.4516 32.29
0.4957 31.43
0.5018 31.43
0.5468 30.41
0.5521 30.40
0.5977 29.18
0.6029 29.14
0.6526 27.62
0.7022 25.75
0.7526 23.41
0.8024 20.54
0.8524 16.98
0.9018 12.65
0.9502 7.47
1.0000 0.92

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 1-Pentanol (2) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 37.19
0.0287 36.63
0.0813 36.21
0.1338 35.77
0.1857 35.31
0.2380 34.81
0.2899 34.27
0.3416 33.69
0.3931 33.04
0.4013 33.04
0.4445 32.30
0.4516 32.29
0.4957 31.43
0.5018 31.43
0.5468 30.41
0.5521 30.40
0.5977 29.18
0.6029 29.14
0.6526 27.62
0.7022 25.75
0.7526 23.41
0.8024 20.54
0.8524 16.98
0.9018 12.65
0.9502 7.47
1.0000 0.92

Sources