Mixture of Cyclohexane + 1,2-Ethanediamine, N,N-diethyl-

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Cyclohexane

Name
Cyclohexane
InChI
InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key
XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula
C6H12
SMILES
C1CCCCC1
Mol. Weight (g/mol)
84.16
CAS
110-82-7

1,2-Ethanediamine, N,N-diethyl-

Name
1,2-Ethanediamine, N,N-diethyl-
InChI
InChI=1S/C6H16N2/c1-3-8(4-2)6-5-7/h3-7H2,1-2H3
InChI Key
UDGSVBYJWHOHNN-UHFFFAOYSA-N
Formula
C6H16N2
SMILES
CCN(CC)CCN
Mol. Weight (g/mol)
116.20
CAS
100-36-7
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)

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

Operational conditions:

Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1053 0.4880
0.2026 0.7700
0.2548 0.8670
0.3243 0.9520
0.3621 0.9740
0.4196 0.9880
Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.5
0.6
0.7
0.8
0.9
1
0.1
0.2
0.30000000000000004
0.4

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

Operational conditions:

Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1053 0.4880
0.2026 0.7700
0.2548 0.8670
0.3243 0.9520
0.3621 0.9740
0.4196 0.9880
Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.5
0.6
0.7
0.8
0.9
1
0.1
0.2
0.30000000000000004
0.4

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
273.15 0.1222 3.38
273.15 0.2567 3.07
273.15 0.3985 2.73
273.15 0.5410 2.32
273.15 0.6788 1.80
273.15 0.8001 1.28
273.15 0.8994 0.78
283.15 0.1222 5.76
283.15 0.2567 5.22
283.15 0.3985 4.62
283.15 0.5410 3.90
283.15 0.6788 3.01
283.15 0.8001 2.15
283.15 0.8994 1.33
293.15 0.1222 9.39
293.15 0.2567 8.51
293.15 0.3985 7.48
293.15 0.5410 6.30
293.15 0.6788 4.85
293.15 0.8001 3.48
293.15 0.8994 2.18
298.15 0.1222 11.82
298.15 0.2567 10.70
298.15 0.3985 9.39
298.15 0.5410 7.90
298.15 0.6788 6.08
298.15 0.8001 4.37
298.15 0.8994 2.76
303.15 0.1222 14.74
303.15 0.2567 13.33
303.15 0.3985 11.68
303.15 0.5410 9.81
303.15 0.6788 7.55
303.15 0.8001 5.44
303.15 0.8994 3.47
313.15 0.1222 22.35
313.15 0.2567 20.19
313.15 0.3985 17.63
313.15 0.5410 14.79
313.15 0.6788 11.39
313.15 0.8001 8.26
313.15 0.8994 5.37
323.15 0.1222 32.89
323.15 0.2567 29.68
323.15 0.3985 25.85
323.15 0.5410 21.65
323.15 0.6788 16.70
323.15 0.8001 12.19
323.15 0.8994 8.08
333.15 0.1222 47.09
333.15 0.2567 42.47
333.15 0.3985 36.90
333.15 0.5410 30.89
333.15 0.6788 23.87
333.15 0.8001 17.56
333.15 0.8994 11.87
343.15 0.1222 65.80
343.15 0.2567 59.30
343.15 0.3985 51.44
343.15 0.5410 43.04
343.15 0.6788 33.35
343.15 0.8001 24.74
343.15 0.8994 17.06
353.15 0.1222 89.93
353.15 0.2567 81.02
353.15 0.3985 70.17
353.15 0.5410 58.70
353.15 0.6788 45.63
353.15 0.8001 34.14
353.15 0.8994 24.02
363.15 0.1222 120.50
363.15 0.2567 108.52
363.15 0.3985 93.87
363.15 0.5410 78.55
363.15 0.6788 61.26
363.15 0.8001 46.23
363.15 0.8994 33.20

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
273.15 0.1222 3.38
273.15 0.2567 3.07
273.15 0.3985 2.73
273.15 0.5410 2.32
273.15 0.6788 1.80
273.15 0.8001 1.28
273.15 0.8994 0.78
283.15 0.1222 5.76
283.15 0.2567 5.22
283.15 0.3985 4.62
283.15 0.5410 3.90
283.15 0.6788 3.01
283.15 0.8001 2.15
283.15 0.8994 1.33
293.15 0.1222 9.39
293.15 0.2567 8.51
293.15 0.3985 7.48
293.15 0.5410 6.30
293.15 0.6788 4.85
293.15 0.8001 3.48
293.15 0.8994 2.18
298.15 0.1222 11.82
298.15 0.2567 10.70
298.15 0.3985 9.39
298.15 0.5410 7.90
298.15 0.6788 6.08
298.15 0.8001 4.37
298.15 0.8994 2.76
303.15 0.1222 14.74
303.15 0.2567 13.33
303.15 0.3985 11.68
303.15 0.5410 9.81
303.15 0.6788 7.55
303.15 0.8001 5.44
303.15 0.8994 3.47
313.15 0.1222 22.35
313.15 0.2567 20.19
313.15 0.3985 17.63
313.15 0.5410 14.79
313.15 0.6788 11.39
313.15 0.8001 8.26
313.15 0.8994 5.37
323.15 0.1222 32.89
323.15 0.2567 29.68
323.15 0.3985 25.85
323.15 0.5410 21.65
323.15 0.6788 16.70
323.15 0.8001 12.19
323.15 0.8994 8.08
333.15 0.1222 47.09
333.15 0.2567 42.47
333.15 0.3985 36.90
333.15 0.5410 30.89
333.15 0.6788 23.87
333.15 0.8001 17.56
333.15 0.8994 11.87
343.15 0.1222 65.80
343.15 0.2567 59.30
343.15 0.3985 51.44
343.15 0.5410 43.04
343.15 0.6788 33.35
343.15 0.8001 24.74
343.15 0.8994 17.06
353.15 0.1222 89.93
353.15 0.2567 81.02
353.15 0.3985 70.17
353.15 0.5410 58.70
353.15 0.6788 45.63
353.15 0.8001 34.14
353.15 0.8994 24.02
363.15 0.1222 120.50
363.15 0.2567 108.52
363.15 0.3985 93.87
363.15 0.5410 78.55
363.15 0.6788 61.26
363.15 0.8001 46.23
363.15 0.8994 33.20

Sources