Mixture of Propane, 1-nitro- + Tridecane

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Propane, 1-nitro-

Name
Propane, 1-nitro-
InChI
InChI=1S/C3H7NO2/c1-2-3-4(5)6/h2-3H2,1H3
InChI Key
JSZOAYXJRCEYSX-UHFFFAOYSA-N
Formula
C3H7NO2
SMILES
CCC[N+](=O)[O-]
Mol. Weight (g/mol)
89.09
CAS
108-03-2

Tridecane

Name
Tridecane
InChI
InChI=1S/C13H28/c1-3-5-7-9-11-13-12-10-8-6-4-2/h3-13H2,1-2H3
InChI Key
IIYFAKIEWZDVMP-UHFFFAOYSA-N
Formula
C13H28
SMILES
CCCCCCCCCCCCC
Mol. Weight (g/mol)
184.36
CAS
629-50-5
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Liquid-liquid equilibrium temperature, K (2)
  3. Excess molar volume, m3/mol (2)

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

Operational conditions:

Mole fraction of Propane, 1-nitro- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.6743 1.817
0.6796 1.811
0.6830 1.792
0.6867 1.785
0.6873 1.781
0.6889 1.775
0.6902 1.767
0.6970 1.75

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

Operational conditions:

Mole fraction of Propane, 1-nitro- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.6743 1.817
0.6796 1.811
0.6830 1.792
0.6867 1.785
0.6873 1.781
0.6889 1.775
0.6902 1.767
0.6970 1.75

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Mole fraction = 0.69 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
393.00 296.24
709.00 296.28
964.00 296.32
1288.00 296.36
1708.00 296.41
2280.00 296.49
3243.00 296.61
3808.00 296.68
4810.00 296.82

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Mole fraction = 0.69 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
393.00 296.24
709.00 296.28
964.00 296.32
1288.00 296.36
1708.00 296.41
2280.00 296.49
3243.00 296.61
3808.00 296.68
4810.00 296.82

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Propane, 1-nitro- (1) - Liquid Excess molar volume, m3/mol - Liquid
0.6792 7.3600e-07
0.6902 7.5300e-07
0.7001 7.7300e-07

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Propane, 1-nitro- (1) - Liquid Excess molar volume, m3/mol - Liquid
0.6792 7.3600e-07
0.6902 7.5300e-07
0.7001 7.7300e-07

Sources