Mixture of Diethyl carbonate + 1-Pentanol

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (6)
3. Excess molar enthalpy (molar enthalpy (2)
4. ρ_l - Mass density, kg/m3 (4)
5. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Diethyl carbonate (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Mole fraction of Diethyl carbonate (1) - Gas
0.0244	0.0566
0.0422	0.0914
0.0689	0.1424
0.1017	0.1974
0.1427	0.2521
0.1818	0.3010
0.2176	0.3467
0.2570	0.3893
0.2892	0.4171
0.3254	0.4506
0.3575	0.4812
0.3885	0.5019
0.4165	0.5297
0.4530	0.5561
0.4870	0.5869
0.5232	0.6136
0.5640	0.6461
0.6056	0.6749
0.6481	0.7043
0.6886	0.7332
0.7457	0.7726
0.7989	0.8140
0.8555	0.8627
0.9128	0.9102
0.9491	0.9451
0.9847	0.9818

Mole fraction of Diethyl carbonate (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Mole fraction of Diethyl carbonate (1) - Gas
0.0244	0.0566
0.0422	0.0914
0.0689	0.1424
0.1017	0.1974
0.1427	0.2521
0.1818	0.3010
0.2176	0.3467
0.2570	0.3893
0.2892	0.4171
0.3254	0.4506
0.3575	0.4812
0.3885	0.5019
0.4165	0.5297
0.4530	0.5561
0.4870	0.5869
0.5232	0.6136
0.5640	0.6461
0.6056	0.6749
0.6481	0.7043
0.6886	0.7332
0.7457	0.7726
0.7989	0.8140
0.8555	0.8627
0.9128	0.9102
0.9491	0.9451
0.9847	0.9818

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0040
293.15	0.0496	0.0034
293.15	0.1016	0.0029
293.15	0.2034	0.0021
293.15	0.3124	0.0016
293.15	0.3801	0.0014
293.15	0.5085	0.0012
293.15	0.6047	0.0011
293.15	0.7068	0.0010
293.15	0.8058	0.0009
293.15	0.9058	0.0008
293.15	0.9521	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0033
298.15	0.0459	0.0029
298.15	0.0984	0.0025
298.15	0.2067	0.0019
298.15	0.3012	0.0015
298.15	0.4002	0.0012
298.15	0.5091	0.0011
298.15	0.5884	0.0010
298.15	0.6988	0.0009
298.15	0.7986	0.0008
298.15	0.9133	0.0008
298.15	0.9663	0.0007
298.15	1.0000	0.0007
303.15	0.0000	0.0029
303.15	0.0541	0.0025
303.15	0.0951	0.0022
303.15	0.1968	0.0017
303.15	0.2920	0.0014
303.15	0.3986	0.0011
303.15	0.4966	0.0010
303.15	0.5963	0.0009
303.15	0.6847	0.0008
303.15	0.7988	0.0007
303.15	0.8885	0.0007
303.15	0.9493	0.0007
303.15	1.0000	0.0007
313.15	0.0000	0.0023
313.15	0.0505	0.0020
313.15	0.1009	0.0017
313.15	0.2038	0.0014
313.15	0.3044	0.0011
313.15	0.4054	0.0010
313.15	0.5077	0.0008
313.15	0.5969	0.0008
313.15	0.7100	0.0007
313.15	0.8100	0.0006
313.15	0.9036	0.0006
313.15	0.9537	0.0006
313.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.1016	0.0029
293.15	0.2056	0.0022
293.15	0.2991	0.0017
298.15	0.1016	0.0025
298.15	0.2056	0.0019
298.15	0.2991	0.0015
303.15	0.1016	0.0022
303.15	0.2056	0.0017
303.15	0.2991	0.0014
313.15	0.1016	0.0017
313.15	0.2056	0.0014
313.15	0.2991	0.0011
323.15	0.1016	0.0014
323.15	0.2056	0.0011
323.15	0.2991	0.0009
333.15	0.1016	0.0011
333.15	0.2056	0.0009
333.15	0.2991	0.0008
343.15	0.1016	0.0009
343.15	0.2056	0.0008
343.15	0.2991	0.0007
353.15	0.1016	0.0008
353.15	0.2056	0.0006
353.15	0.2991	0.0006
363.15	0.1016	0.0006
363.15	0.2056	0.0006
363.15	0.2991	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0503	0.0039
288.15	0.1060	0.0032
288.15	0.1881	0.0025
288.15	0.2879	0.0020
288.15	0.3960	0.0016
288.15	0.4905	0.0014
288.15	0.5917	0.0012
288.15	0.7104	0.0010
288.15	0.8067	0.0009
288.15	0.8960	0.0009
288.15	0.9607	0.0009
293.15	0.0485	0.0034
293.15	0.0572	0.0033
293.15	0.1071	0.0028
293.15	0.1988	0.0021
293.15	0.2900	0.0017
293.15	0.3980	0.0014
293.15	0.4939	0.0012
293.15	0.5998	0.0010
293.15	0.6968	0.0009
293.15	0.8009	0.0009
293.15	0.8902	0.0008
293.15	0.9604	0.0008
303.15	0.0625	0.0025
303.15	0.0998	0.0022
303.15	0.2017	0.0017
303.15	0.2898	0.0014
303.15	0.3969	0.0012
303.15	0.4922	0.0010
303.15	0.5941	0.0009
303.15	0.6987	0.0008
303.15	0.8039	0.0008
303.15	0.8997	0.0007
303.15	0.9608	0.0007
313.15	0.0541	0.0020
313.15	0.1042	0.0017
313.15	0.1939	0.0014
313.15	0.2900	0.0011
313.15	0.4060	0.0009
313.15	0.4965	0.0008
313.15	0.5957	0.0008
313.15	0.7474	0.0007
313.15	0.8030	0.0007
313.15	0.8997	0.0006
313.15	0.9582	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0040
293.15	0.0496	0.0034
293.15	0.1016	0.0029
293.15	0.2034	0.0021
293.15	0.3124	0.0016
293.15	0.3801	0.0014
293.15	0.5085	0.0012
293.15	0.6047	0.0011
293.15	0.7068	0.0010
293.15	0.8058	0.0009
293.15	0.9058	0.0008
293.15	0.9521	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0033
298.15	0.0459	0.0029
298.15	0.0984	0.0025
298.15	0.2067	0.0019
298.15	0.3012	0.0015
298.15	0.4002	0.0012
298.15	0.5091	0.0011
298.15	0.5884	0.0010
298.15	0.6988	0.0009
298.15	0.7986	0.0008
298.15	0.9133	0.0008
298.15	0.9663	0.0007
298.15	1.0000	0.0007
303.15	0.0000	0.0029
303.15	0.0541	0.0025
303.15	0.0951	0.0022
303.15	0.1968	0.0017
303.15	0.2920	0.0014
303.15	0.3986	0.0011
303.15	0.4966	0.0010
303.15	0.5963	0.0009
303.15	0.6847	0.0008
303.15	0.7988	0.0007
303.15	0.8885	0.0007
303.15	0.9493	0.0007
303.15	1.0000	0.0007
313.15	0.0000	0.0023
313.15	0.0505	0.0020
313.15	0.1009	0.0017
313.15	0.2038	0.0014
313.15	0.3044	0.0011
313.15	0.4054	0.0010
313.15	0.5077	0.0008
313.15	0.5969	0.0008
313.15	0.7100	0.0007
313.15	0.8100	0.0006
313.15	0.9036	0.0006
313.15	0.9537	0.0006
313.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.1016	0.0029
293.15	0.2056	0.0022
293.15	0.2991	0.0017
298.15	0.1016	0.0025
298.15	0.2056	0.0019
298.15	0.2991	0.0015
303.15	0.1016	0.0022
303.15	0.2056	0.0017
303.15	0.2991	0.0014
313.15	0.1016	0.0017
313.15	0.2056	0.0014
313.15	0.2991	0.0011
323.15	0.1016	0.0014
323.15	0.2056	0.0011
323.15	0.2991	0.0009
333.15	0.1016	0.0011
333.15	0.2056	0.0009
333.15	0.2991	0.0008
343.15	0.1016	0.0009
343.15	0.2056	0.0008
343.15	0.2991	0.0007
353.15	0.1016	0.0008
353.15	0.2056	0.0006
353.15	0.2991	0.0006
363.15	0.1016	0.0006
363.15	0.2056	0.0006
363.15	0.2991	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0503	0.0039
288.15	0.1060	0.0032
288.15	0.1881	0.0025
288.15	0.2879	0.0020
288.15	0.3960	0.0016
288.15	0.4905	0.0014
288.15	0.5917	0.0012
288.15	0.7104	0.0010
288.15	0.8067	0.0009
288.15	0.8960	0.0009
288.15	0.9607	0.0009
293.15	0.0485	0.0034
293.15	0.0572	0.0033
293.15	0.1071	0.0028
293.15	0.1988	0.0021
293.15	0.2900	0.0017
293.15	0.3980	0.0014
293.15	0.4939	0.0012
293.15	0.5998	0.0010
293.15	0.6968	0.0009
293.15	0.8009	0.0009
293.15	0.8902	0.0008
293.15	0.9604	0.0008
303.15	0.0625	0.0025
303.15	0.0998	0.0022
303.15	0.2017	0.0017
303.15	0.2898	0.0014
303.15	0.3969	0.0012
303.15	0.4922	0.0010
303.15	0.5941	0.0009
303.15	0.6987	0.0008
303.15	0.8039	0.0008
303.15	0.8997	0.0007
303.15	0.9608	0.0007
313.15	0.0541	0.0020
313.15	0.1042	0.0017
313.15	0.1939	0.0014
313.15	0.2900	0.0011
313.15	0.4060	0.0009
313.15	0.4965	0.0008
313.15	0.5957	0.0008
313.15	0.7474	0.0007
313.15	0.8030	0.0007
313.15	0.8997	0.0006
313.15	0.9582	0.0006

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

Operational conditions:

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

Mole fraction of Diethyl carbonate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0484	0.3831
0.0850	0.6545
0.1521	1.0515
0.2122	1.3629
0.2630	1.562
0.3154	1.7473
0.3592	1.8451
0.4399	1.9942
0.4581	1.9981
0.5444	2.0553
0.6400	1.9654
0.6925	1.8203
0.7415	1.7032
0.7993	1.4949
0.8519	1.2195
0.9139	0.7984

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

Operational conditions:

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

Mole fraction of Diethyl carbonate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0484	0.3831
0.0850	0.6545
0.1521	1.0515
0.2122	1.3629
0.2630	1.562
0.3154	1.7473
0.3592	1.8451
0.4399	1.9942
0.4581	1.9981
0.5444	2.0553
0.6400	1.9654
0.6925	1.8203
0.7415	1.7032
0.7993	1.4949
0.8519	1.2195
0.9139	0.7984

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.1016	831.8
293.15	0.2056	849.16
293.15	0.2991	864.58
298.15	0.1016	827.59
298.15	0.2056	844.75
298.15	0.2991	859.91
303.15	0.1016	823.06
303.15	0.2056	840.03
303.15	0.2991	854.97
313.15	0.1016	814.72
313.15	0.2056	831.26
313.15	0.2991	845.78
323.15	0.1016	805.16
323.15	0.2056	821.48
323.15	0.2991	835.87
333.15	0.1016	796.72
333.15	0.2056	812.44
333.15	0.2991	826.67
343.15	0.1016	787.31
343.15	0.2056	802.62
343.15	0.2991	816.48
353.15	0.1016	778.85
353.15	0.2056	793.74
353.15	0.2991	807.26
363.15	0.1016	770.78
363.15	0.2056	785.19
363.15	0.2991	798.3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0503	826.9
288.15	0.1060	836.4
288.15	0.1881	850.28
288.15	0.2879	866.92
288.15	0.3960	884.69
288.15	0.4905	900.03
288.15	0.5917	916.28
288.15	0.7104	935.09
288.15	0.8067	950.23
288.15	0.8960	964.17
288.15	0.9607	974.25
293.15	0.0485	822.8
293.15	0.0572	824.25
293.15	0.1071	832.6
293.15	0.1988	847.85
293.15	0.2900	862.87
293.15	0.3980	880.41
293.15	0.4939	895.79
293.15	0.5998	912.55
293.15	0.6968	927.7
293.15	0.8009	943.91
293.15	0.8902	957.76
293.15	0.9604	968.66
303.15	0.0625	817.46
303.15	0.0998	823.53
303.15	0.2017	839.99
303.15	0.2898	854.09
303.15	0.3969	871.0
303.15	0.4922	885.91
303.15	0.5941	901.64
303.15	0.6987	917.65
303.15	0.8039	933.63
303.15	0.8997	948.13
303.15	0.9608	957.42
313.15	0.0541	808.37
313.15	0.1042	816.28
313.15	0.1939	830.39
313.15	0.2900	845.34
313.15	0.4060	863.19
313.15	0.4965	876.96
313.15	0.5957	891.9
313.15	0.7474	914.56
313.15	0.8030	922.81
313.15	0.8997	937.15
313.15	0.9582	945.86

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.1016	831.8
293.15	0.2056	849.16
293.15	0.2991	864.58
298.15	0.1016	827.59
298.15	0.2056	844.75
298.15	0.2991	859.91
303.15	0.1016	823.06
303.15	0.2056	840.03
303.15	0.2991	854.97
313.15	0.1016	814.72
313.15	0.2056	831.26
313.15	0.2991	845.78
323.15	0.1016	805.16
323.15	0.2056	821.48
323.15	0.2991	835.87
333.15	0.1016	796.72
333.15	0.2056	812.44
333.15	0.2991	826.67
343.15	0.1016	787.31
343.15	0.2056	802.62
343.15	0.2991	816.48
353.15	0.1016	778.85
353.15	0.2056	793.74
353.15	0.2991	807.26
363.15	0.1016	770.78
363.15	0.2056	785.19
363.15	0.2991	798.3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0503	826.9
288.15	0.1060	836.4
288.15	0.1881	850.28
288.15	0.2879	866.92
288.15	0.3960	884.69
288.15	0.4905	900.03
288.15	0.5917	916.28
288.15	0.7104	935.09
288.15	0.8067	950.23
288.15	0.8960	964.17
288.15	0.9607	974.25
293.15	0.0485	822.8
293.15	0.0572	824.25
293.15	0.1071	832.6
293.15	0.1988	847.85
293.15	0.2900	862.87
293.15	0.3980	880.41
293.15	0.4939	895.79
293.15	0.5998	912.55
293.15	0.6968	927.7
293.15	0.8009	943.91
293.15	0.8902	957.76
293.15	0.9604	968.66
303.15	0.0625	817.46
303.15	0.0998	823.53
303.15	0.2017	839.99
303.15	0.2898	854.09
303.15	0.3969	871.0
303.15	0.4922	885.91
303.15	0.5941	901.64
303.15	0.6987	917.65
303.15	0.8039	933.63
303.15	0.8997	948.13
303.15	0.9608	957.42
313.15	0.0541	808.37
313.15	0.1042	816.28
313.15	0.1939	830.39
313.15	0.2900	845.34
313.15	0.4060	863.19
313.15	0.4965	876.96
313.15	0.5957	891.9
313.15	0.7474	914.56
313.15	0.8030	922.81
313.15	0.8997	937.15
313.15	0.9582	945.86

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0244	410.19
0.0422	409.57
0.0689	408.71
0.1017	407.69
0.1427	406.71
0.1818	405.87
0.2176	405.12
0.2570	404.45
0.2892	404.00
0.3254	403.54
0.3575	403.09
0.3885	402.80
0.4165	402.42
0.4530	402.06
0.4870	401.70
0.5232	401.37
0.5640	401.02
0.6056	400.67
0.6481	400.36
0.6886	400.06
0.7457	399.75
0.7989	399.52
0.8555	399.28
0.9128	399.18
0.9491	399.20
0.9847	399.29

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0244	410.19
0.0422	409.57
0.0689	408.71
0.1017	407.69
0.1427	406.71
0.1818	405.87
0.2176	405.12
0.2570	404.45
0.2892	404.00
0.3254	403.54
0.3575	403.09
0.3885	402.80
0.4165	402.42
0.4530	402.06
0.4870	401.70
0.5232	401.37
0.5640	401.02
0.6056	400.67
0.6481	400.36
0.6886	400.06
0.7457	399.75
0.7989	399.52
0.8555	399.28
0.9128	399.18
0.9491	399.20
0.9847	399.29

Sources

• Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
• Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
• Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
• Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K