Mixture of Propane, 1-nitro- + Decane

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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

Decane

Name
Decane
InChI
InChI=1S/C10H22/c1-3-5-7-9-10-8-6-4-2/h3-10H2,1-2H3
InChI Key
DIOQZVSQGTUSAI-UHFFFAOYSA-N
Formula
C10H22
SMILES
CCCCCCCCCC
Mol. Weight (g/mol)
142.28
CAS
124-18-5
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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
0.5521 1.716
0.5615 1.744
0.5661 1.748
0.5664 1.748
0.5746 1.745
0.5825 1.744
0.5915 1.738
0.5915 1.726
Mole fraction of Propane, 1-nitro- (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
1.72
1.72
1.73
1.73
1.74
1.74
1.75
1.75
0.56
0.5700000000000001
0.5800000000000001
0.5900000000000001

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
0.5521 1.716
0.5615 1.744
0.5661 1.748
0.5664 1.748
0.5746 1.745
0.5825 1.744
0.5915 1.738
0.5915 1.726
Mole fraction of Propane, 1-nitro- (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
1.72
1.72
1.73
1.73
1.74
1.74
1.75
1.75
0.56
0.5700000000000001
0.5800000000000001
0.5900000000000001

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Mole fraction = 0.571 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
316.00 281.69
605.00 281.71
811.00 281.73
1198.00 281.78
1424.00 281.80
1897.00 281.84
2505.00 281.89
3121.00 281.96
4226.00 282.07
Pressure, kPa
Liquid-liquid equilibrium temperature, K
281.7
281.8
281.9
282
282.1
1000
2000
3000
4000

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Mole fraction = 0.571 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
316.00 281.69
605.00 281.71
811.00 281.73
1198.00 281.78
1424.00 281.80
1897.00 281.84
2505.00 281.89
3121.00 281.96
4226.00 282.07
Pressure, kPa
Liquid-liquid equilibrium temperature, K
281.7
281.8
281.9
282
282.1
1000
2000
3000
4000

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
0.5803 5.5200e-07
0.5901 5.5000e-07
0.6003 5.4700e-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
0.5803 5.5200e-07
0.5901 5.5000e-07
0.6003 5.4700e-07

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