Mixture of 1-Hexene + 2-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

2-Pentanol

Name
2-Pentanol
InChI
InChI=1S/C5H12O/c1-3-4-5(2)6/h5-6H,3-4H2,1-2H3
InChI Key
JYVLIDXNZAXMDK-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCC(C)O
Mol. Weight (g/mol)
88.15
CAS
6032-29-7
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Datasets

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

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

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (2) - Liquid Mole fraction of 2-Pentanol (2) - Gas
0.0000 0.0000
0.0498 0.0147
0.1004 0.0203
0.1502 0.0235
0.2007 0.0263
0.2521 0.0290
0.3011 0.0316
0.3513 0.0344
0.4013 0.0372
0.4015 0.0372
0.4514 0.0401
0.4516 0.0401
0.5016 0.0434
0.5018 0.0434
0.5514 0.0471
0.5519 0.0471
0.6014 0.0515
0.6022 0.0516
0.6522 0.0571
0.7024 0.0641
0.7523 0.0736
0.8022 0.0872
0.8520 0.1088
0.9018 0.1497
0.9509 0.2531
1.0000 1.0000

Mole fraction of 1-Hexene (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of 1-Hexene (1) - Liquid Mole fraction of 1-Hexene (1) - Gas
0.0170 0.1400
0.0320 0.2680
0.0560 0.3950
0.1000 0.5680
0.1250 0.6260
0.1500 0.6780
0.2150 0.7780
0.2820 0.8340
0.3440 0.8730
0.3950 0.8920
0.4560 0.9100
0.5150 0.9230
0.5770 0.9330
0.6280 0.9400
0.6810 0.9470
0.7340 0.9530
0.7890 0.9580
0.8410 0.9610
0.8950 0.9710
0.9490 0.9830
0.9830 0.9940

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

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (2) - Liquid Mole fraction of 2-Pentanol (2) - Gas
0.0000 0.0000
0.0498 0.0147
0.1004 0.0203
0.1502 0.0235
0.2007 0.0263
0.2521 0.0290
0.3011 0.0316
0.3513 0.0344
0.4013 0.0372
0.4015 0.0372
0.4514 0.0401
0.4516 0.0401
0.5016 0.0434
0.5018 0.0434
0.5514 0.0471
0.5519 0.0471
0.6014 0.0515
0.6022 0.0516
0.6522 0.0571
0.7024 0.0641
0.7523 0.0736
0.8022 0.0872
0.8520 0.1088
0.9018 0.1497
0.9509 0.2531
1.0000 1.0000

Mole fraction of 1-Hexene (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of 1-Hexene (1) - Liquid Mole fraction of 1-Hexene (1) - Gas
0.0170 0.1400
0.0320 0.2680
0.0560 0.3950
0.1000 0.5680
0.1250 0.6260
0.1500 0.6780
0.2150 0.7780
0.2820 0.8340
0.3440 0.8730
0.3950 0.8920
0.4560 0.9100
0.5150 0.9230
0.5770 0.9330
0.6280 0.9400
0.6810 0.9470
0.7340 0.9530
0.7890 0.9580
0.8410 0.9610
0.8950 0.9710
0.9490 0.9830
0.9830 0.9940

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Pentanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0503 0.4887
298.15 0.0999 0.6592
298.15 0.1511 0.7665
298.15 0.2015 0.8453
298.15 0.2513 0.9017
298.15 0.3027 0.9404
298.15 0.3512 0.9634
298.15 0.4032 0.9792
298.15 0.4525 0.9788
298.15 0.5030 0.9622
298.15 0.5529 0.9282
298.15 0.6018 0.8769
298.15 0.6523 0.8108
298.15 0.7020 0.7311
298.15 0.7510 0.6306
298.15 0.8004 0.5139
298.15 0.8500 0.3914
298.15 0.9007 0.2400
298.15 0.9507 0.1123
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0500 0.5895
313.15 0.0999 0.8210
313.15 0.1512 0.9570
313.15 0.2017 1.0608
313.15 0.2516 1.1136
313.15 0.3028 1.16
313.15 0.3513 1.179
313.15 0.4034 1.1817
313.15 0.4509 1.163
313.15 0.5014 1.1357
313.15 0.5513 1.0947
313.15 0.6005 1.0365
313.15 0.6523 0.9499
313.15 0.7020 0.8598
313.15 0.7510 0.7518
313.15 0.8012 0.6225
313.15 0.8506 0.4804
313.15 0.9012 0.3104
313.15 0.9509 0.1551
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 2-Pentanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0503 0.4887
298.15 0.0999 0.6592
298.15 0.1511 0.7665
298.15 0.2015 0.8453
298.15 0.2513 0.9017
298.15 0.3027 0.9404
298.15 0.3512 0.9634
298.15 0.4032 0.9792
298.15 0.4525 0.9788
298.15 0.5030 0.9622
298.15 0.5529 0.9282
298.15 0.6018 0.8769
298.15 0.6523 0.8108
298.15 0.7020 0.7311
298.15 0.7510 0.6306
298.15 0.8004 0.5139
298.15 0.8500 0.3914
298.15 0.9007 0.2400
298.15 0.9507 0.1123
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0500 0.5895
313.15 0.0999 0.8210
313.15 0.1512 0.9570
313.15 0.2017 1.0608
313.15 0.2516 1.1136
313.15 0.3028 1.16
313.15 0.3513 1.179
313.15 0.4034 1.1817
313.15 0.4509 1.163
313.15 0.5014 1.1357
313.15 0.5513 1.0947
313.15 0.6005 1.0365
313.15 0.6523 0.9499
313.15 0.7020 0.8598
313.15 0.7510 0.7518
313.15 0.8012 0.6225
313.15 0.8506 0.4804
313.15 0.9012 0.3104
313.15 0.9509 0.1551
313.15 1.0000 0.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of 1-Hexene (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0170 388.05
0.0320 384.92
0.0560 380.13
0.1000 373.28
0.1250 369.17
0.1500 366.41
0.2150 359.50
0.2820 354.51
0.3440 351.19
0.3950 348.56
0.4560 346.34
0.5150 344.39
0.5770 342.90
0.6280 341.85
0.6810 340.71
0.7340 339.87
0.7890 339.14
0.8410 338.40
0.8950 337.71
0.9490 337.00
0.9830 336.63

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of 1-Hexene (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0170 388.05
0.0320 384.92
0.0560 380.13
0.1000 373.28
0.1250 369.17
0.1500 366.41
0.2150 359.50
0.2820 354.51
0.3440 351.19
0.3950 348.56
0.4560 346.34
0.5150 344.39
0.5770 342.90
0.6280 341.85
0.6810 340.71
0.7340 339.87
0.7890 339.14
0.8410 338.40
0.8950 337.71
0.9490 337.00
0.9830 336.63

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (2) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 44.95
0.0498 43.92
0.1004 43.13
0.1502 42.45
0.2007 41.71
0.2521 40.86
0.3011 39.95
0.3513 38.94
0.4013 37.85
0.4015 37.84
0.4514 36.67
0.4516 36.66
0.5016 35.36
0.5018 35.35
0.5514 33.89
0.5519 33.87
0.6014 32.19
0.6022 32.17
0.6522 30.22
0.7024 27.94
0.7523 25.29
0.8022 22.18
0.8520 18.48
0.9018 14.00
0.9509 8.63
1.0000 2.28

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (2) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 44.95
0.0498 43.92
0.1004 43.13
0.1502 42.45
0.2007 41.71
0.2521 40.86
0.3011 39.95
0.3513 38.94
0.4013 37.85
0.4015 37.84
0.4514 36.67
0.4516 36.66
0.5016 35.36
0.5018 35.35
0.5514 33.89
0.5519 33.87
0.6014 32.19
0.6022 32.17
0.6522 30.22
0.7024 27.94
0.7523 25.29
0.8022 22.18
0.8520 18.48
0.9018 14.00
0.9509 8.63
1.0000 2.28

Sources