Mixture of 1-Hexene + 1-Pentanol

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1-Hexene

Name
1-Hexene
InChI
InChI=1S/C6H12/c1-3-5-6-4-2/h3H,1,4-6H2,2H3
InChI Key
LIKMAJRDDDTEIG-UHFFFAOYSA-N
Formula
C6H12
SMILES
C=CCCCC
Mol. Weight (g/mol)
84.16
CAS
592-41-6

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 (2)
  3. Vapor or sublimation pressure, kPa (2)

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

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 1-Pentanol (2) - Liquid Mole fraction of 1-Pentanol (2) - Gas
0.0000 0.0000
0.0492 0.0075
0.0995 0.0096
0.1503 0.0106
0.2007 0.0115
0.2511 0.0124
0.3014 0.0133
0.3516 0.0142
0.4014 0.0151
0.4016 0.0151
0.4517 0.0161
0.4518 0.0161
0.5017 0.0171
0.5019 0.0171
0.5517 0.0184
0.5521 0.0184
0.6021 0.0200
0.6024 0.0200
0.6527 0.0220
0.7025 0.0247
0.7528 0.0284
0.8028 0.0338
0.8526 0.0428
0.8999 0.0593
0.9493 0.1072
1.0000 1.0000

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

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 1-Pentanol (2) - Liquid Mole fraction of 1-Pentanol (2) - Gas
0.0000 0.0000
0.0492 0.0075
0.0995 0.0096
0.1503 0.0106
0.2007 0.0115
0.2511 0.0124
0.3014 0.0133
0.3516 0.0142
0.4014 0.0151
0.4016 0.0151
0.4517 0.0161
0.4518 0.0161
0.5017 0.0171
0.5019 0.0171
0.5517 0.0184
0.5521 0.0184
0.6021 0.0200
0.6024 0.0200
0.6527 0.0220
0.7025 0.0247
0.7528 0.0284
0.8028 0.0338
0.8526 0.0428
0.8999 0.0593
0.9493 0.1072
1.0000 1.0000

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 0.0507 0.3974
298.15 0.1006 0.4978
298.15 0.1522 0.5602
298.15 0.2030 0.5981
298.15 0.2531 0.6196
298.15 0.3022 0.6303
298.15 0.3530 0.6266
298.15 0.4030 0.6108
298.15 0.4523 0.5794
298.15 0.5030 0.5404
298.15 0.5529 0.4952
298.15 0.6040 0.4437
298.15 0.6523 0.3817
298.15 0.7019 0.3248
298.15 0.7526 0.2633
298.15 0.8008 0.1999
298.15 0.8482 0.1458
298.15 0.9020 0.0871
298.15 0.9513 0.0380
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0506 0.5076
313.15 0.1005 0.6640
313.15 0.1520 0.7493
313.15 0.2027 0.8024
313.15 0.2528 0.8159
313.15 0.3021 0.8290
313.15 0.3526 0.8072
313.15 0.4026 0.7948
313.15 0.4519 0.7639
313.15 0.5026 0.7179
313.15 0.5524 0.6664
313.15 0.6035 0.6032
313.15 0.6519 0.5314
313.15 0.7019 0.4568
313.15 0.7526 0.3716
313.15 0.8025 0.2848
313.15 0.8517 0.2114
313.15 0.9019 0.1323
313.15 0.9513 0.0581
313.15 1.0000 0.0000

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 0.0507 0.3974
298.15 0.1006 0.4978
298.15 0.1522 0.5602
298.15 0.2030 0.5981
298.15 0.2531 0.6196
298.15 0.3022 0.6303
298.15 0.3530 0.6266
298.15 0.4030 0.6108
298.15 0.4523 0.5794
298.15 0.5030 0.5404
298.15 0.5529 0.4952
298.15 0.6040 0.4437
298.15 0.6523 0.3817
298.15 0.7019 0.3248
298.15 0.7526 0.2633
298.15 0.8008 0.1999
298.15 0.8482 0.1458
298.15 0.9020 0.0871
298.15 0.9513 0.0380
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0506 0.5076
313.15 0.1005 0.6640
313.15 0.1520 0.7493
313.15 0.2027 0.8024
313.15 0.2528 0.8159
313.15 0.3021 0.8290
313.15 0.3526 0.8072
313.15 0.4026 0.7948
313.15 0.4519 0.7639
313.15 0.5026 0.7179
313.15 0.5524 0.6664
313.15 0.6035 0.6032
313.15 0.6519 0.5314
313.15 0.7019 0.4568
313.15 0.7526 0.3716
313.15 0.8025 0.2848
313.15 0.8517 0.2114
313.15 0.9019 0.1323
313.15 0.9513 0.0581
313.15 1.0000 0.0000

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 44.91
0.0492 43.85
0.0995 43.19
0.1503 42.55
0.2007 41.89
0.2511 41.18
0.3014 40.45
0.3516 39.62
0.4014 38.75
0.4016 38.71
0.4517 37.72
0.4518 37.67
0.5017 36.49
0.5019 36.53
0.5517 35.10
0.5521 35.14
0.6021 33.45
0.6024 33.50
0.6527 31.53
0.7025 29.17
0.7528 26.30
0.8028 22.87
0.8526 18.72
0.8999 14.05
0.9493 8.16
1.0000 0.91

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 44.91
0.0492 43.85
0.0995 43.19
0.1503 42.55
0.2007 41.89
0.2511 41.18
0.3014 40.45
0.3516 39.62
0.4014 38.75
0.4016 38.71
0.4517 37.72
0.4518 37.67
0.5017 36.49
0.5019 36.53
0.5517 35.10
0.5521 35.14
0.6021 33.45
0.6024 33.50
0.6527 31.53
0.7025 29.17
0.7528 26.30
0.8028 22.87
0.8526 18.72
0.8999 14.05
0.9493 8.16
1.0000 0.91

Sources