Mixture of Toluene + 1-Pentanol

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Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

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

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

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid Mole fraction of 1-Pentanol (2) - Gas
0.0000 0.0000
0.0493 0.0283
0.0991 0.0428
0.1495 0.0513
0.1997 0.0571
0.2495 0.0620
0.2995 0.0667
0.3497 0.0716
0.3997 0.0770
0.4049 0.0776
0.4497 0.0829
0.4551 0.0836
0.4996 0.0896
0.5052 0.0904
0.5497 0.0972
0.5551 0.0981
0.5997 0.1062
0.6050 0.1073
0.6548 0.1184
0.7046 0.1326
0.7539 0.1514
0.8040 0.1788
0.8532 0.2211
0.9023 0.2953
0.9517 0.4571
1.0000 1.0000

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

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid Mole fraction of 1-Pentanol (2) - Gas
0.0000 0.0000
0.0493 0.0283
0.0991 0.0428
0.1495 0.0513
0.1997 0.0571
0.2495 0.0620
0.2995 0.0667
0.3497 0.0716
0.3997 0.0770
0.4049 0.0776
0.4497 0.0829
0.4551 0.0836
0.4996 0.0896
0.5052 0.0904
0.5497 0.0972
0.5551 0.0981
0.5997 0.1062
0.6050 0.1073
0.6548 0.1184
0.7046 0.1326
0.7539 0.1514
0.8040 0.1788
0.8532 0.2211
0.9023 0.2953
0.9517 0.4571
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 0.0511 0.5393
298.15 0.1004 0.7603
298.15 0.1497 0.8839
298.15 0.2012 0.9726
298.15 0.2507 1.0212
298.15 0.3003 1.0481
298.15 0.3500 1.0627
298.15 0.4018 1.0423
298.15 0.4516 1.0107
298.15 0.5016 0.9595
298.15 0.5517 0.8937
298.15 0.6018 0.8160
298.15 0.6500 0.7281
298.15 0.7003 0.6324
298.15 0.7507 0.5289
298.15 0.8012 0.4149
298.15 0.8497 0.3125
298.15 0.9004 0.2031
298.15 0.9491 0.1015
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0511 0.5964
313.15 0.1004 0.8837
313.15 0.1498 1.0533
313.15 0.2013 1.1688
313.15 0.2508 1.2314
313.15 0.3003 1.2511
313.15 0.3500 1.2524
313.15 0.3999 1.2536
313.15 0.4518 1.2026
313.15 0.5016 1.157
313.15 0.5517 1.0893
313.15 0.6019 1.0027
313.15 0.6501 0.9042
313.15 0.7004 0.7937
313.15 0.7508 0.6669
313.15 0.8013 0.5402
313.15 0.8498 0.4092
313.15 0.9005 0.2670
313.15 0.9492 0.1320
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 0.0511 0.5393
298.15 0.1004 0.7603
298.15 0.1497 0.8839
298.15 0.2012 0.9726
298.15 0.2507 1.0212
298.15 0.3003 1.0481
298.15 0.3500 1.0627
298.15 0.4018 1.0423
298.15 0.4516 1.0107
298.15 0.5016 0.9595
298.15 0.5517 0.8937
298.15 0.6018 0.8160
298.15 0.6500 0.7281
298.15 0.7003 0.6324
298.15 0.7507 0.5289
298.15 0.8012 0.4149
298.15 0.8497 0.3125
298.15 0.9004 0.2031
298.15 0.9491 0.1015
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0511 0.5964
313.15 0.1004 0.8837
313.15 0.1498 1.0533
313.15 0.2013 1.1688
313.15 0.2508 1.2314
313.15 0.3003 1.2511
313.15 0.3500 1.2524
313.15 0.3999 1.2536
313.15 0.4518 1.2026
313.15 0.5016 1.157
313.15 0.5517 1.0893
313.15 0.6019 1.0027
313.15 0.6501 0.9042
313.15 0.7004 0.7937
313.15 0.7508 0.6669
313.15 0.8013 0.5402
313.15 0.8498 0.4092
313.15 0.9005 0.2670
313.15 0.9492 0.1320
313.15 1.0000 0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 7.86
0.0493 7.79
0.0991 7.70
0.1495 7.59
0.1997 7.49
0.2495 7.37
0.2995 7.23
0.3497 7.08
0.3997 6.92
0.4049 6.92
0.4497 6.72
0.4551 6.72
0.4996 6.51
0.5052 6.52
0.5497 6.27
0.5551 6.27
0.5997 5.97
0.6050 5.97
0.6548 5.64
0.7046 5.23
0.7539 4.76
0.8040 4.20
0.8532 3.56
0.9023 2.80
0.9517 1.92
1.0000 0.90

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 7.86
0.0493 7.79
0.0991 7.70
0.1495 7.59
0.1997 7.49
0.2495 7.37
0.2995 7.23
0.3497 7.08
0.3997 6.92
0.4049 6.92
0.4497 6.72
0.4551 6.72
0.4996 6.51
0.5052 6.52
0.5497 6.27
0.5551 6.27
0.5997 5.97
0.6050 5.97
0.6548 5.64
0.7046 5.23
0.7539 4.76
0.8040 4.20
0.8532 3.56
0.9023 2.80
0.9517 1.92
1.0000 0.90

Sources