Mixture of 1-Propanol + 1-Hexene

Excel

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

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
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ρl - Mass density, kg/m3 (2)

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-Hexene (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0501 0.0610
298.15 0.1003 0.1260
298.15 0.1501 0.1920
298.15 0.2002 0.2560
298.15 0.2501 0.3190
298.15 0.3004 0.3820
298.15 0.3501 0.4420
298.15 0.4007 0.4980
298.15 0.4501 0.5520
298.15 0.5001 0.5950
298.15 0.5504 0.6340
298.15 0.5998 0.6640
298.15 0.6505 0.6830
298.15 0.6998 0.6900
298.15 0.7500 0.6820
298.15 0.7999 0.6590
298.15 0.8505 0.6160
298.15 0.9004 0.5480
298.15 0.9508 0.4270
313.15 0.0501 0.0920
313.15 0.1002 0.1860
313.15 0.1501 0.2790
313.15 0.2001 0.3700
313.15 0.2499 0.4570
313.15 0.3003 0.5420
313.15 0.3499 0.6210
313.15 0.4006 0.6950
313.15 0.4499 0.7580
313.15 0.4998 0.8140
313.15 0.5502 0.8600
313.15 0.5996 0.8940
313.15 0.6503 0.9140
313.15 0.6996 0.9190
313.15 0.7500 0.9070
313.15 0.7998 0.8750
313.15 0.8505 0.8150
313.15 0.9004 0.7210
313.15 0.9508 0.5470

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-Hexene (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0501 0.0610
298.15 0.1003 0.1260
298.15 0.1501 0.1920
298.15 0.2002 0.2560
298.15 0.2501 0.3190
298.15 0.3004 0.3820
298.15 0.3501 0.4420
298.15 0.4007 0.4980
298.15 0.4501 0.5520
298.15 0.5001 0.5950
298.15 0.5504 0.6340
298.15 0.5998 0.6640
298.15 0.6505 0.6830
298.15 0.6998 0.6900
298.15 0.7500 0.6820
298.15 0.7999 0.6590
298.15 0.8505 0.6160
298.15 0.9004 0.5480
298.15 0.9508 0.4270
313.15 0.0501 0.0920
313.15 0.1002 0.1860
313.15 0.1501 0.2790
313.15 0.2001 0.3700
313.15 0.2499 0.4570
313.15 0.3003 0.5420
313.15 0.3499 0.6210
313.15 0.4006 0.6950
313.15 0.4499 0.7580
313.15 0.4998 0.8140
313.15 0.5502 0.8600
313.15 0.5996 0.8940
313.15 0.6503 0.9140
313.15 0.6996 0.9190
313.15 0.7500 0.9070
313.15 0.7998 0.8750
313.15 0.8505 0.8150
313.15 0.9004 0.7210
313.15 0.9508 0.5470

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of 1-Propanol (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 668.28
0.0559 672.355
0.1058 676.386
0.1507 680.245
0.1992 684.668
0.2544 689.977
0.3009 694.674
0.3520 700.098
0.3964 705.058
0.5009 717.645
0.5518 724.304
0.6016 731.083
0.7038 746.106
0.8088 763.299
0.8497 770.498
0.8990 779.526
0.9490 789.187
1.0000 799.651

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of 1-Propanol (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 668.28
0.0559 672.355
0.1058 676.386
0.1507 680.245
0.1992 684.668
0.2544 689.977
0.3009 694.674
0.3520 700.098
0.3964 705.058
0.5009 717.645
0.5518 724.304
0.6016 731.083
0.7038 746.106
0.8088 763.299
0.8497 770.498
0.8990 779.526
0.9490 789.187
1.0000 799.651

Sources