Mixture of 1-Octene + 1-Hexanol

Excel

1-Octene

Name
1-Octene
InChI
InChI=1S/C8H16/c1-3-5-7-8-6-4-2/h3H,1,4-8H2,2H3
InChI Key
KWKAKUADMBZCLK-UHFFFAOYSA-N
Formula
C8H16
SMILES
C=CCCCCCC
Mol. Weight (g/mol)
112.21
CAS
111-66-0

1-Hexanol

Name
1-Hexanol
InChI
InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
InChI Key
ZSIAUFGUXNUGDI-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCCCCO
Mol. Weight (g/mol)
102.17
CAS
111-27-3
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Excess molar volume, m3/mol (2)

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

Operational conditions:

Mole fraction of 1-Hexanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0960 0.3353
0.1920 0.4399
0.3070 0.5019
0.4030 0.4919
0.5000 0.4439
0.5980 0.3814
0.6970 0.3029
0.8020 0.2056
0.9000 0.0973

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

Operational conditions:

Mole fraction of 1-Hexanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0960 0.3353
0.1920 0.4399
0.3070 0.5019
0.4030 0.4919
0.5000 0.4439
0.5980 0.3814
0.6970 0.3029
0.8020 0.2056
0.9000 0.0973

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Hexanol (2) - Liquid Excess molar volume, m3/mol - Liquid
288.15 0.0497 3.6000e-08
288.15 0.1102 3.8000e-08
288.15 0.1609 4.3000e-08
288.15 0.2071 4.0000e-08
288.15 0.2578 3.6000e-08
288.15 0.3054 2.1000e-08
288.15 0.3536 0.0000
288.15 0.4550 -1.4000e-08
288.15 0.5035 -2.6000e-08
288.15 0.5414 -4.0000e-08
288.15 0.6010 -5.0000e-08
288.15 0.6471 -6.1000e-08
288.15 0.7063 -7.6000e-08
288.15 0.7556 -7.4000e-08
288.15 0.8008 -7.8000e-08
288.15 0.8489 -7.1000e-08
288.15 0.8977 -5.3000e-08
288.15 0.9475 -3.5000e-08
308.15 0.1177 8.8000e-08
308.15 0.1732 9.0000e-08
308.15 0.2182 8.3000e-08
308.15 0.2670 7.8000e-08
308.15 0.3158 6.4000e-08
308.15 0.3672 4.3000e-08
308.15 0.4135 3.2000e-08
308.15 0.4866 0.0000
308.15 0.5308 -1.1000e-08
308.15 0.5899 -3.3000e-08
308.15 0.6361 -4.5000e-08
308.15 0.6920 -6.1000e-08
308.15 0.7521 -6.7000e-08
308.15 0.7991 -7.2000e-08
308.15 0.8499 -6.3000e-08
308.15 0.8993 -4.9000e-08
308.15 0.9479 -2.7000e-08

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Hexanol (2) - Liquid Excess molar volume, m3/mol - Liquid
288.15 0.0497 3.6000e-08
288.15 0.1102 3.8000e-08
288.15 0.1609 4.3000e-08
288.15 0.2071 4.0000e-08
288.15 0.2578 3.6000e-08
288.15 0.3054 2.1000e-08
288.15 0.3536 0.0000
288.15 0.4550 -1.4000e-08
288.15 0.5035 -2.6000e-08
288.15 0.5414 -4.0000e-08
288.15 0.6010 -5.0000e-08
288.15 0.6471 -6.1000e-08
288.15 0.7063 -7.6000e-08
288.15 0.7556 -7.4000e-08
288.15 0.8008 -7.8000e-08
288.15 0.8489 -7.1000e-08
288.15 0.8977 -5.3000e-08
288.15 0.9475 -3.5000e-08
308.15 0.1177 8.8000e-08
308.15 0.1732 9.0000e-08
308.15 0.2182 8.3000e-08
308.15 0.2670 7.8000e-08
308.15 0.3158 6.4000e-08
308.15 0.3672 4.3000e-08
308.15 0.4135 3.2000e-08
308.15 0.4866 0.0000
308.15 0.5308 -1.1000e-08
308.15 0.5899 -3.3000e-08
308.15 0.6361 -4.5000e-08
308.15 0.6920 -6.1000e-08
308.15 0.7521 -6.7000e-08
308.15 0.7991 -7.2000e-08
308.15 0.8499 -6.3000e-08
308.15 0.8993 -4.9000e-08
308.15 0.9479 -2.7000e-08

Sources