Mixture of 2-Pentanol + Benzene, 1,2,4-trimethyl-

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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

Benzene, 1,2,4-trimethyl-

Name
Benzene, 1,2,4-trimethyl-
InChI
InChI=1S/C9H12/c1-7-4-5-8(2)9(3)6-7/h4-6H,1-3H3
InChI Key
GWHJZXXIDMPWGX-UHFFFAOYSA-N
Formula
C9H12
SMILES
Cc1ccc(C)c(C)c1
Mol. Weight (g/mol)
120.19
CAS
95-63-6
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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 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
0.0504 0.4515
0.1002 0.5566
0.1504 0.6065
0.2000 0.6378
0.2509 0.6619
0.3010 0.6816
0.3512 0.6993
0.4000 0.7154
0.4015 0.7159
0.4499 0.7313
0.4515 0.7318
0.5000 0.7470
0.5016 0.7475
0.5500 0.7626
0.5517 0.7631
0.5999 0.7781
0.6016 0.7787
0.6499 0.7939
0.7000 0.8103
0.7501 0.8282
0.8000 0.8489
0.8501 0.8747
0.9003 0.9079
0.9504 0.9506
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
0.0504 0.4515
0.1002 0.5566
0.1504 0.6065
0.2000 0.6378
0.2509 0.6619
0.3010 0.6816
0.3512 0.6993
0.4000 0.7154
0.4015 0.7159
0.4499 0.7313
0.4515 0.7318
0.5000 0.7470
0.5016 0.7475
0.5500 0.7626
0.5517 0.7631
0.5999 0.7781
0.6016 0.7787
0.6499 0.7939
0.7000 0.8103
0.7501 0.8282
0.8000 0.8489
0.8501 0.8747
0.9003 0.9079
0.9504 0.9506
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 0.0499 0.6012
298.15 0.1012 0.9111
298.15 0.1490 1.1032
298.15 0.2006 1.2409
298.15 0.2487 1.3457
298.15 0.2980 1.4155
298.15 0.3485 1.4662
298.15 0.3979 1.4965
298.15 0.4482 1.508
298.15 0.4996 1.4896
298.15 0.5496 1.459
298.15 0.6006 1.3964
298.15 0.6502 1.3102
298.15 0.6988 1.2081
298.15 0.7480 1.0825
298.15 0.7979 0.9217
298.15 0.8482 0.7343
298.15 0.8990 0.5194
298.15 0.9502 0.2709
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0499 0.6219
313.15 0.0987 0.9919
313.15 0.1490 1.2352
313.15 0.1982 1.3956
313.15 0.2509 1.5084
313.15 0.3002 1.5981
313.15 0.3507 1.641
313.15 0.3979 1.668
313.15 0.4504 1.6728
313.15 0.4996 1.6601
313.15 0.5476 1.6156
313.15 0.6005 1.5454
313.15 0.6482 1.4496
313.15 0.6987 1.3319
313.15 0.7479 1.1914
313.15 0.7978 1.0162
313.15 0.8481 0.8112
313.15 0.8989 0.5780
313.15 0.9501 0.3003
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 0.0499 0.6012
298.15 0.1012 0.9111
298.15 0.1490 1.1032
298.15 0.2006 1.2409
298.15 0.2487 1.3457
298.15 0.2980 1.4155
298.15 0.3485 1.4662
298.15 0.3979 1.4965
298.15 0.4482 1.508
298.15 0.4996 1.4896
298.15 0.5496 1.459
298.15 0.6006 1.3964
298.15 0.6502 1.3102
298.15 0.6988 1.2081
298.15 0.7480 1.0825
298.15 0.7979 0.9217
298.15 0.8482 0.7343
298.15 0.8990 0.5194
298.15 0.9502 0.2709
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0499 0.6219
313.15 0.0987 0.9919
313.15 0.1490 1.2352
313.15 0.1982 1.3956
313.15 0.2509 1.5084
313.15 0.3002 1.5981
313.15 0.3507 1.641
313.15 0.3979 1.668
313.15 0.4504 1.6728
313.15 0.4996 1.6601
313.15 0.5476 1.6156
313.15 0.6005 1.5454
313.15 0.6482 1.4496
313.15 0.6987 1.3319
313.15 0.7479 1.1914
313.15 0.7978 1.0162
313.15 0.8481 0.8112
313.15 0.8989 0.5780
313.15 0.9501 0.3003
313.15 1.0000 0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (1) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 0.73
0.0504 1.23
0.1002 1.48
0.1504 1.62
0.2000 1.72
0.2509 1.80
0.3010 1.86
0.3512 1.93
0.4000 1.97
0.4015 1.98
0.4499 2.02
0.4515 2.01
0.5000 2.07
0.5016 2.08
0.5500 2.09
0.5517 2.13
0.5999 2.13
0.6016 2.15
0.6499 2.17
0.7000 2.21
0.7501 2.24
0.8000 2.24
0.8501 2.27
0.9003 2.28
0.9504 2.28
1.0000 2.27

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (1) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 0.73
0.0504 1.23
0.1002 1.48
0.1504 1.62
0.2000 1.72
0.2509 1.80
0.3010 1.86
0.3512 1.93
0.4000 1.97
0.4015 1.98
0.4499 2.02
0.4515 2.01
0.5000 2.07
0.5016 2.08
0.5500 2.09
0.5517 2.13
0.5999 2.13
0.6016 2.15
0.6499 2.17
0.7000 2.21
0.7501 2.24
0.8000 2.24
0.8501 2.27
0.9003 2.28
0.9504 2.28
1.0000 2.27

Sources