Mixture of Propane, 1-nitro- + Dodecane

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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

Dodecane

Name
Dodecane
InChI
InChI=1S/C12H26/c1-3-5-7-9-11-12-10-8-6-4-2/h3-12H2,1-2H3
InChI Key
SNRUBQQJIBEYMU-UHFFFAOYSA-N
Formula
C12H26
SMILES
CCCCCCCCCCCC
Mol. Weight (g/mol)
170.33
CAS
112-40-3
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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
0.6231 1.794
0.6281 1.783
0.6502 1.759
0.6574 1.748
0.6689 1.73
0.6726 1.714
0.6759 1.706

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
0.6231 1.794
0.6281 1.783
0.6502 1.759
0.6574 1.748
0.6689 1.73
0.6726 1.714
0.6759 1.706

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Mole fraction = 0.661 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
340.00 292.07
444.00 292.56
523.00 292.09
789.00 292.13
947.00 292.14
1383.00 292.20
1754.00 292.25
2284.00 292.31
2851.00 292.38
3480.00 292.44
3867.00 292.50

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Mole fraction = 0.661 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
340.00 292.07
444.00 292.56
523.00 292.09
789.00 292.13
947.00 292.14
1383.00 292.20
1754.00 292.25
2284.00 292.31
2851.00 292.38
3480.00 292.44
3867.00 292.50

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
0.6503 6.8400e-07
0.6606 6.6900e-07
0.6704 6.7300e-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
0.6503 6.8400e-07
0.6606 6.6900e-07
0.6704 6.7300e-07

Sources