Mixture of 1,3-Propanediamine, N,N-diethyl- + Cyclohexane

Datasets

1. Excess molar enthalpy (molar enthalpy (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. Excess molar volume, m3/mol (2)

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1022	0.5900
0.2027	0.8740
0.3028	1.024
0.3197	1.034
0.3519	1.051
0.3953	1.068
0.4070	1.074
0.4449	1.075
0.4943	1.064
0.5061	1.065
0.5307	1.038
0.5351	1.037
0.5595	1.017
0.5741	0.9980
0.6073	0.9520
0.6523	0.8790
0.7017	0.7840
0.7997	0.5480
0.8696	0.3500

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1022	0.5900
0.2027	0.8740
0.3028	1.024
0.3197	1.034
0.3519	1.051
0.3953	1.068
0.4070	1.074
0.4449	1.075
0.4943	1.064
0.5061	1.065
0.5307	1.038
0.5351	1.037
0.5595	1.017
0.5741	0.9980
0.6073	0.9520
0.6523	0.8790
0.7017	0.7840
0.7997	0.5480
0.8696	0.3500

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1013	273.15	3.43
0.1013	283.15	5.84
0.1013	293.15	9.52
0.1013	303.15	14.92
0.1013	313.15	22.59
0.1013	323.15	33.17
0.1013	333.15	47.41
0.1013	343.15	66.06
0.1013	353.15	90.08
0.1013	363.15	120.38
0.2177	273.15	3.12
0.2177	283.15	5.31
0.2177	293.15	8.65
0.2177	303.15	13.54
0.2177	313.15	20.48
0.2177	323.15	30.03
0.2177	333.15	42.72
0.2177	343.15	59.66
0.2177	353.15	81.24
0.2177	363.15	108.86
0.3209	273.15	2.89
0.3209	283.15	4.86
0.3209	293.15	7.84
0.3209	303.15	12.19
0.3209	313.15	18.34
0.3209	323.15	26.80
0.3209	333.15	38.34
0.3209	343.15	53.03
0.3209	353.15	72.16
0.3209	363.15	96.31
0.4535	273.15	2.51
0.4535	283.15	4.21
0.4535	293.15	6.75
0.4535	303.15	10.46
0.4535	313.15	15.66
0.4535	323.15	22.79
0.4535	333.15	32.22
0.4535	343.15	44.71
0.4535	353.15	60.60
0.4535	363.15	80.57
0.6559	273.15	1.77
0.6559	283.15	2.93
0.6559	293.15	4.66
0.6559	303.15	7.16
0.6559	313.15	10.67
0.6559	323.15	15.55
0.6559	333.15	21.75
0.6559	343.15	30.15
0.6559	353.15	40.79
0.6559	363.15	54.17
0.8455	273.15	0.87
0.8455	283.15	1.42
0.8455	293.15	2.26
0.8455	303.15	3.48
0.8455	313.15	5.21
0.8455	323.15	7.61
0.8455	333.15	11.00
0.8455	343.15	15.21
0.8455	353.15	20.87
0.8455	363.15	28.13

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1013	273.15	3.43
0.1013	283.15	5.84
0.1013	293.15	9.52
0.1013	303.15	14.92
0.1013	313.15	22.59
0.1013	323.15	33.17
0.1013	333.15	47.41
0.1013	343.15	66.06
0.1013	353.15	90.08
0.1013	363.15	120.38
0.2177	273.15	3.12
0.2177	283.15	5.31
0.2177	293.15	8.65
0.2177	303.15	13.54
0.2177	313.15	20.48
0.2177	323.15	30.03
0.2177	333.15	42.72
0.2177	343.15	59.66
0.2177	353.15	81.24
0.2177	363.15	108.86
0.3209	273.15	2.89
0.3209	283.15	4.86
0.3209	293.15	7.84
0.3209	303.15	12.19
0.3209	313.15	18.34
0.3209	323.15	26.80
0.3209	333.15	38.34
0.3209	343.15	53.03
0.3209	353.15	72.16
0.3209	363.15	96.31
0.4535	273.15	2.51
0.4535	283.15	4.21
0.4535	293.15	6.75
0.4535	303.15	10.46
0.4535	313.15	15.66
0.4535	323.15	22.79
0.4535	333.15	32.22
0.4535	343.15	44.71
0.4535	353.15	60.60
0.4535	363.15	80.57
0.6559	273.15	1.77
0.6559	283.15	2.93
0.6559	293.15	4.66
0.6559	303.15	7.16
0.6559	313.15	10.67
0.6559	323.15	15.55
0.6559	333.15	21.75
0.6559	343.15	30.15
0.6559	353.15	40.79
0.6559	363.15	54.17
0.8455	273.15	0.87
0.8455	283.15	1.42
0.8455	293.15	2.26
0.8455	303.15	3.48
0.8455	313.15	5.21
0.8455	323.15	7.61
0.8455	333.15	11.00
0.8455	343.15	15.21
0.8455	353.15	20.87
0.8455	363.15	28.13

Excess molar volume, m3/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.1130	4.5930e-07
0.2100	6.7620e-07
0.3035	7.8040e-07
0.4030	8.0160e-07
0.4990	7.5670e-07
0.6008	6.7850e-07
0.7025	5.3620e-07
0.7965	3.6920e-07
0.8911	2.5450e-07

Excess molar volume, m3/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.1130	4.5930e-07
0.2100	6.7620e-07
0.3035	7.8040e-07
0.4030	8.0160e-07
0.4990	7.5670e-07
0.6008	6.7850e-07
0.7025	5.3620e-07
0.7965	3.6920e-07
0.8911	2.5450e-07

Sources

• Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}