Mixture of Propane, 1-nitro- + Tetradecane

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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

Tetradecane

Name
Tetradecane
InChI
InChI=1S/C14H30/c1-3-5-7-9-11-13-14-12-10-8-6-4-2/h3-14H2,1-2H3
InChI Key
BGHCVCJVXZWKCC-UHFFFAOYSA-N
Formula
C14H30
SMILES
CCCCCCCCCCCCCC
Mol. Weight (g/mol)
198.39
CAS
629-59-4
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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
0.6886 1.83
0.6918 1.831
0.6924 1.831
0.7024 1.806
0.7032 1.814
0.7058 1.787
0.7083 1.778
0.7117 1.762
Mole fraction of Propane, 1-nitro- (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
1.76
1.77
1.78
1.79
1.8
1.81
1.82
1.83
0.6900000000000001
0.7000000000000001
0.7100000000000001

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
0.6886 1.83
0.6918 1.831
0.6924 1.831
0.7024 1.806
0.7032 1.814
0.7058 1.787
0.7083 1.778
0.7117 1.762
Mole fraction of Propane, 1-nitro- (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
1.76
1.77
1.78
1.79
1.8
1.81
1.82
1.83
0.6900000000000001
0.7000000000000001
0.7100000000000001

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Mole fraction = 0.7 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
485.00 300.81
831.00 300.86
1157.00 300.90
1552.00 300.96
2151.00 301.04
2513.00 301.09
3929.00 301.28
4677.00 301.38
Pressure, kPa
Liquid-liquid equilibrium temperature, K
300.8
300.9
301
301.1
301.2
301.3
301.4
1000
2000
3000
4000

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Mole fraction = 0.7 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
485.00 300.81
831.00 300.86
1157.00 300.90
1552.00 300.96
2151.00 301.04
2513.00 301.09
3929.00 301.28
4677.00 301.38
Pressure, kPa
Liquid-liquid equilibrium temperature, K
300.8
300.9
301
301.1
301.2
301.3
301.4
1000
2000
3000
4000

Excess molar volume, m3/mol [ref]

Fixed Measured
Mole fraction of Propane, 1-nitro- (1) - Liquid Pressure, kPa - Liquid Excess molar volume, m3/mol - Liquid
0.7089 101.00 7.7300e-07

Excess molar volume, m3/mol [ref]

Fixed Measured
Mole fraction of Propane, 1-nitro- (1) - Liquid Pressure, kPa - Liquid Excess molar volume, m3/mol - Liquid
0.7089 101.00 7.7300e-07

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