Mixture of 2-Pentanol + Heptane

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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

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)

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

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (1) - Liquid Mole fraction of 2-Pentanol (1) - Gas
0.0000 0.0000
0.0493 0.0593
0.0991 0.0776
0.1491 0.0870
0.1989 0.0946
0.2490 0.1020
0.2991 0.1094
0.3490 0.1168
0.3990 0.1243
0.3990 0.1243
0.4490 0.1318
0.4491 0.1319
0.4990 0.1398
0.4991 0.1399
0.5491 0.1487
0.5493 0.1487
0.5991 0.1589
0.5994 0.1590
0.6494 0.1713
0.6995 0.1866
0.7499 0.2067
0.8000 0.2342
0.8502 0.2755
0.9001 0.3460
0.9504 0.4972
1.0000 1.0000

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

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (1) - Liquid Mole fraction of 2-Pentanol (1) - Gas
0.0000 0.0000
0.0493 0.0593
0.0991 0.0776
0.1491 0.0870
0.1989 0.0946
0.2490 0.1020
0.2991 0.1094
0.3490 0.1168
0.3990 0.1243
0.3990 0.1243
0.4490 0.1318
0.4491 0.1319
0.4990 0.1398
0.4991 0.1399
0.5491 0.1487
0.5493 0.1487
0.5991 0.1589
0.5994 0.1590
0.6494 0.1713
0.6995 0.1866
0.7499 0.2067
0.8000 0.2342
0.8502 0.2755
0.9001 0.3460
0.9504 0.4972
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 2-Pentanol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0505 0.4890
298.15 0.0997 0.6302
298.15 0.1477 0.7253
298.15 0.1969 0.7954
298.15 0.2472 0.8488
298.15 0.2962 0.8820
298.15 0.3460 0.9169
298.15 0.3967 0.9394
298.15 0.4459 0.9500
298.15 0.4958 0.9463
298.15 0.5463 0.9252
298.15 0.5972 0.8887
298.15 0.6466 0.8350
298.15 0.6963 0.7592
298.15 0.7480 0.6647
298.15 0.7981 0.5540
298.15 0.8483 0.4313
298.15 0.8985 0.2954
298.15 0.9486 0.1500
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0504 0.6117
313.15 0.0996 0.8255
313.15 0.1475 0.9335
313.15 0.1967 1.0143
313.15 0.2469 1.0697
313.15 0.2956 1.1106
313.15 0.3455 1.1307
313.15 0.3962 1.1439
313.15 0.4454 1.1422
313.15 0.4953 1.1303
313.15 0.5458 1.0986
313.15 0.5968 1.051
313.15 0.6462 0.9926
313.15 0.6959 0.8950
313.15 0.7477 0.7943
313.15 0.7979 0.6728
313.15 0.8481 0.5299
313.15 0.8984 0.3681
313.15 0.9485 0.1929
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 (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0505 0.4890
298.15 0.0997 0.6302
298.15 0.1477 0.7253
298.15 0.1969 0.7954
298.15 0.2472 0.8488
298.15 0.2962 0.8820
298.15 0.3460 0.9169
298.15 0.3967 0.9394
298.15 0.4459 0.9500
298.15 0.4958 0.9463
298.15 0.5463 0.9252
298.15 0.5972 0.8887
298.15 0.6466 0.8350
298.15 0.6963 0.7592
298.15 0.7480 0.6647
298.15 0.7981 0.5540
298.15 0.8483 0.4313
298.15 0.8985 0.2954
298.15 0.9486 0.1500
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0504 0.6117
313.15 0.0996 0.8255
313.15 0.1475 0.9335
313.15 0.1967 1.0143
313.15 0.2469 1.0697
313.15 0.2956 1.1106
313.15 0.3455 1.1307
313.15 0.3962 1.1439
313.15 0.4454 1.1422
313.15 0.4953 1.1303
313.15 0.5458 1.0986
313.15 0.5968 1.051
313.15 0.6462 0.9926
313.15 0.6959 0.8950
313.15 0.7477 0.7943
313.15 0.7979 0.6728
313.15 0.8481 0.5299
313.15 0.8984 0.3681
313.15 0.9485 0.1929
313.15 1.0000 0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 2-Pentanol (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 12.31
0.0493 12.66
0.0991 12.66
0.1491 12.57
0.1989 12.46
0.2490 12.34
0.2991 12.18
0.3490 11.99
0.3990 11.79
0.3990 11.80
0.4490 11.53
0.4491 11.55
0.4990 11.25
0.4991 11.29
0.5491 10.96
0.5493 10.98
0.5991 10.60
0.5994 10.62
0.6494 10.19
0.6995 9.68
0.7499 8.99
0.8000 8.27
0.8502 7.29
0.9001 6.01
0.9504 4.39
1.0000 2.30

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 2-Pentanol (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 12.31
0.0493 12.66
0.0991 12.66
0.1491 12.57
0.1989 12.46
0.2490 12.34
0.2991 12.18
0.3490 11.99
0.3990 11.79
0.3990 11.80
0.4490 11.53
0.4491 11.55
0.4990 11.25
0.4991 11.29
0.5491 10.96
0.5493 10.98
0.5991 10.60
0.5994 10.62
0.6494 10.19
0.6995 9.68
0.7499 8.99
0.8000 8.27
0.8502 7.29
0.9001 6.01
0.9504 4.39
1.0000 2.30

Sources