Mixture of Octane + Acetic acid, methyl ester

Excel

Octane

Name
Octane
InChI
InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3
InChI Key
TVMXDCGIABBOFY-UHFFFAOYSA-N
Formula
C8H18
SMILES
CCCCCCCC
Mol. Weight (g/mol)
114.23
CAS
111-65-9

Acetic acid, methyl ester

Name
Acetic acid, methyl ester
InChI
InChI=1S/C3H6O2/c1-3(4)5-2/h1-2H3
InChI Key
KXKVLQRXCPHEJC-UHFFFAOYSA-N
Formula
C3H6O2
SMILES
COC(C)=O
Mol. Weight (g/mol)
74.08
CAS
79-20-9
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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 conditions:

Mole fraction of Octane (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0466 0.4150
0.1009 0.8130
0.1504 1.135
0.2057 1.415
0.2580 1.634
0.3043 1.786
0.3516 1.905
0.3642 1.943
0.3999 2.005
0.4460 2.039
0.5006 2.038
0.5742 1.955
0.6631 1.743
0.7615 1.384
0.8485 0.9450
0.9324 0.4480

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

Operational conditions:

Mole fraction of Octane (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0466 0.4150
0.1009 0.8130
0.1504 1.135
0.2057 1.415
0.2580 1.634
0.3043 1.786
0.3516 1.905
0.3642 1.943
0.3999 2.005
0.4460 2.039
0.5006 2.038
0.5742 1.955
0.6631 1.743
0.7615 1.384
0.8485 0.9450
0.9324 0.4480

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Octane (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 927.16
0.0493 901.46
0.1011 878.04
0.1517 857.91
0.2033 839.55
0.2530 823.66
0.3008 809.86
0.3471 797.79
0.3946 786.15
0.4523 773.45
0.4951 764.76
0.5307 758.11
0.5777 749.93
0.5898 747.92
0.6146 743.98
0.6388 740.27
0.6699 735.52
0.7238 728.1
0.7841 720.49
0.8333 714.64
0.8887 708.75
0.9311 704.69
0.9585 702.21
1.0000 698.58

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Octane (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 927.16
0.0493 901.46
0.1011 878.04
0.1517 857.91
0.2033 839.55
0.2530 823.66
0.3008 809.86
0.3471 797.79
0.3946 786.15
0.4523 773.45
0.4951 764.76
0.5307 758.11
0.5777 749.93
0.5898 747.92
0.6146 743.98
0.6388 740.27
0.6699 735.52
0.7238 728.1
0.7841 720.49
0.8333 714.64
0.8887 708.75
0.9311 704.69
0.9585 702.21
1.0000 698.58

Sources