Mixture of Diethyl carbonate + Ethanol

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (4)
3. Excess molar enthalpy (molar enthalpy (2)
4. P_c - Critical pressure, kPa (2)
5. P_vap - Vapor or sublimation pressure, kPa (2)
6. n₀ - Refractive index (Na D-line) (4)
7. ρ_l - Mass density, kg/m3 (6)
8. c_sound,fluid - Speed of Sound, m/s (4)
9. T_boil - Boiling temperature at pressure P, K (2)
10. T_c - Critical temperature, K (2)

Mole fraction of Ethanol (2) [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol (2) - Gas
0.0000	353.15	0.0000
0.0404	353.15	0.3969
0.0974	353.15	0.6259
0.1972	353.15	0.7582
0.2974	353.15	0.8145
0.4029	353.15	0.8445
0.4980	353.15	0.8645
0.5990	353.15	0.8829
0.6992	353.15	0.8994
0.8004	353.15	0.9189
0.8999	353.15	0.9484
0.9502	353.15	0.9705
1.0000	353.15	1.0000
0.0000	363.15	0.0000
0.0510	363.15	0.4497
0.1005	363.15	0.5932
0.2007	363.15	0.7407
0.2984	363.15	0.8018
0.4039	363.15	0.8227
0.4984	363.15	0.8346
0.5987	363.15	0.8593
0.6987	363.15	0.8881
0.8008	363.15	0.9109
0.9003	363.15	0.9432
0.9504	363.15	0.9684
1.0000	363.15	1.0000

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
0.0157	0.1093
0.0315	0.2018
0.0464	0.2756
0.0671	0.3658
0.0851	0.4344
0.1061	0.4949
0.1341	0.5635
0.1615	0.6169
0.1951	0.6659
0.2195	0.6924
0.2472	0.7219
0.2725	0.7409
0.3070	0.7658
0.3425	0.7855
0.3796	0.8026
0.4168	0.8175
0.4524	0.8303
0.4836	0.8414
0.5018	0.8462
0.5395	0.8587
0.5633	0.8658
0.6074	0.8787
0.6464	0.8901
0.6905	0.9018
0.7282	0.9123
0.7895	0.9267
0.8222	0.9350
0.8528	0.9425
0.8828	0.9484
0.9112	0.9576
0.9331	0.9660
0.9541	0.9745
0.9649	0.9800
0.9861	0.9918

Mole fraction of Ethanol (2) [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol (2) - Gas
0.0000	353.15	0.0000
0.0404	353.15	0.3969
0.0974	353.15	0.6259
0.1972	353.15	0.7582
0.2974	353.15	0.8145
0.4029	353.15	0.8445
0.4980	353.15	0.8645
0.5990	353.15	0.8829
0.6992	353.15	0.8994
0.8004	353.15	0.9189
0.8999	353.15	0.9484
0.9502	353.15	0.9705
1.0000	353.15	1.0000
0.0000	363.15	0.0000
0.0510	363.15	0.4497
0.1005	363.15	0.5932
0.2007	363.15	0.7407
0.2984	363.15	0.8018
0.4039	363.15	0.8227
0.4984	363.15	0.8346
0.5987	363.15	0.8593
0.6987	363.15	0.8881
0.8008	363.15	0.9109
0.9003	363.15	0.9432
0.9504	363.15	0.9684
1.0000	363.15	1.0000

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
0.0157	0.1093
0.0315	0.2018
0.0464	0.2756
0.0671	0.3658
0.0851	0.4344
0.1061	0.4949
0.1341	0.5635
0.1615	0.6169
0.1951	0.6659
0.2195	0.6924
0.2472	0.7219
0.2725	0.7409
0.3070	0.7658
0.3425	0.7855
0.3796	0.8026
0.4168	0.8175
0.4524	0.8303
0.4836	0.8414
0.5018	0.8462
0.5395	0.8587
0.5633	0.8658
0.6074	0.8787
0.6464	0.8901
0.6905	0.9018
0.7282	0.9123
0.7895	0.9267
0.8222	0.9350
0.8528	0.9425
0.8828	0.9484
0.9112	0.9576
0.9331	0.9660
0.9541	0.9745
0.9649	0.9800
0.9861	0.9918

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	0.0012
293.15	0.0503	0.0011
293.15	0.0997	0.0010
293.15	0.1980	0.0009
293.15	0.3006	0.0008
293.15	0.4031	0.0008
293.15	0.5031	0.0008
293.15	0.6063	0.0008
293.15	0.6898	0.0008
293.15	0.8066	0.0008
293.15	0.8950	0.0008
293.15	0.9450	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0011
298.15	0.0496	0.0010
298.15	0.0973	0.0009
298.15	0.1963	0.0008
298.15	0.2985	0.0008
298.15	0.3980	0.0007
298.15	0.5057	0.0007
298.15	0.6032	0.0007
298.15	0.7035	0.0007
298.15	0.7999	0.0007
298.15	0.8989	0.0007
298.15	0.9283	0.0007
298.15	1.0000	0.0007
303.15	0.0000	0.0010
303.15	0.0491	0.0009
303.15	0.0984	0.0008
303.15	0.1952	0.0008
303.15	0.2961	0.0007
303.15	0.3946	0.0007
303.15	0.4859	0.0007
303.15	0.5995	0.0006
303.15	0.6959	0.0006
303.15	0.7862	0.0006
303.15	0.8911	0.0007
303.15	0.9254	0.0007
303.15	1.0000	0.0007
313.15	0.0000	0.0008
313.15	0.0499	0.0008
313.15	0.1020	0.0007
313.15	0.2038	0.0007
313.15	0.3116	0.0006
313.15	0.4001	0.0006
313.15	0.4971	0.0006
313.15	0.6023	0.0006
313.15	0.7058	0.0006
313.15	0.8065	0.0006
313.15	0.9022	0.0006
313.15	0.9518	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
288.15	0.0554	0.0012
288.15	0.1000	0.0011
288.15	0.1970	0.0010
288.15	0.2998	0.0009
288.15	0.4062	0.0009
288.15	0.5039	0.0008
288.15	0.6130	0.0008
288.15	0.6939	0.0008
288.15	0.7942	0.0008
288.15	0.8992	0.0008
288.15	0.9744	0.0009
293.15	0.0521	0.0011
293.15	0.0964	0.0010
293.15	0.1983	0.0009
293.15	0.2931	0.0009
293.15	0.4089	0.0008
293.15	0.4945	0.0008
293.15	0.6111	0.0008
293.15	0.6787	0.0008
293.15	0.7692	0.0008
293.15	0.8767	0.0008
293.15	0.9444	0.0008
303.15	0.0459	0.0009
303.15	0.0969	0.0009
303.15	0.1943	0.0008
303.15	0.2843	0.0007
303.15	0.4098	0.0007
303.15	0.5128	0.0007
303.15	0.6176	0.0007
303.15	0.6907	0.0007
303.15	0.7896	0.0007
303.15	0.8863	0.0007
303.15	0.9676	0.0007
313.15	0.0496	0.0008
313.15	0.0965	0.0007
313.15	0.2070	0.0006
313.15	0.2847	0.0006
313.15	0.3982	0.0006
313.15	0.5049	0.0006
313.15	0.6079	0.0006
313.15	0.6227	0.0006
313.15	0.6895	0.0006
313.15	0.7826	0.0006
313.15	0.8924	0.0006
313.15	0.9563	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	0.0012
293.15	0.0503	0.0011
293.15	0.0997	0.0010
293.15	0.1980	0.0009
293.15	0.3006	0.0008
293.15	0.4031	0.0008
293.15	0.5031	0.0008
293.15	0.6063	0.0008
293.15	0.6898	0.0008
293.15	0.8066	0.0008
293.15	0.8950	0.0008
293.15	0.9450	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0011
298.15	0.0496	0.0010
298.15	0.0973	0.0009
298.15	0.1963	0.0008
298.15	0.2985	0.0008
298.15	0.3980	0.0007
298.15	0.5057	0.0007
298.15	0.6032	0.0007
298.15	0.7035	0.0007
298.15	0.7999	0.0007
298.15	0.8989	0.0007
298.15	0.9283	0.0007
298.15	1.0000	0.0007
303.15	0.0000	0.0010
303.15	0.0491	0.0009
303.15	0.0984	0.0008
303.15	0.1952	0.0008
303.15	0.2961	0.0007
303.15	0.3946	0.0007
303.15	0.4859	0.0007
303.15	0.5995	0.0006
303.15	0.6959	0.0006
303.15	0.7862	0.0006
303.15	0.8911	0.0007
303.15	0.9254	0.0007
303.15	1.0000	0.0007
313.15	0.0000	0.0008
313.15	0.0499	0.0008
313.15	0.1020	0.0007
313.15	0.2038	0.0007
313.15	0.3116	0.0006
313.15	0.4001	0.0006
313.15	0.4971	0.0006
313.15	0.6023	0.0006
313.15	0.7058	0.0006
313.15	0.8065	0.0006
313.15	0.9022	0.0006
313.15	0.9518	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
288.15	0.0554	0.0012
288.15	0.1000	0.0011
288.15	0.1970	0.0010
288.15	0.2998	0.0009
288.15	0.4062	0.0009
288.15	0.5039	0.0008
288.15	0.6130	0.0008
288.15	0.6939	0.0008
288.15	0.7942	0.0008
288.15	0.8992	0.0008
288.15	0.9744	0.0009
293.15	0.0521	0.0011
293.15	0.0964	0.0010
293.15	0.1983	0.0009
293.15	0.2931	0.0009
293.15	0.4089	0.0008
293.15	0.4945	0.0008
293.15	0.6111	0.0008
293.15	0.6787	0.0008
293.15	0.7692	0.0008
293.15	0.8767	0.0008
293.15	0.9444	0.0008
303.15	0.0459	0.0009
303.15	0.0969	0.0009
303.15	0.1943	0.0008
303.15	0.2843	0.0007
303.15	0.4098	0.0007
303.15	0.5128	0.0007
303.15	0.6176	0.0007
303.15	0.6907	0.0007
303.15	0.7896	0.0007
303.15	0.8863	0.0007
303.15	0.9676	0.0007
313.15	0.0496	0.0008
313.15	0.0965	0.0007
313.15	0.2070	0.0006
313.15	0.2847	0.0006
313.15	0.3982	0.0006
313.15	0.5049	0.0006
313.15	0.6079	0.0006
313.15	0.6227	0.0006
313.15	0.6895	0.0006
313.15	0.7826	0.0006
313.15	0.8924	0.0006
313.15	0.9563	0.0006

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

Operational conditions:

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

Mole fraction of Diethyl carbonate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0643	0.3945
0.1113	0.6373
0.1833	0.9438
0.2439	1.1547
0.3034	1.3252
0.3739	1.488
0.4258	1.5806
0.5066	1.6536
0.5445	1.6519
0.6400	1.6299
0.7134	1.5293
0.7663	1.4031
0.8243	1.1939
0.8998	0.7905
0.9557	0.3957

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

Operational conditions:

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

Mole fraction of Diethyl carbonate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0643	0.3945
0.1113	0.6373
0.1833	0.9438
0.2439	1.1547
0.3034	1.3252
0.3739	1.488
0.4258	1.5806
0.5066	1.6536
0.5445	1.6519
0.6400	1.6299
0.7134	1.5293
0.7663	1.4031
0.8243	1.1939
0.8998	0.7905
0.9557	0.3957

Critical pressure, kPa [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical pressure, kPa - Liquid
0.0415	6053.00
0.0888	5965.00
0.1432	5852.00
0.2063	5732.00
0.2806	5538.00
0.3691	5319.00
0.4764	5004.00
0.6094	4546.00
0.7783	3787.00

Critical pressure, kPa [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical pressure, kPa - Liquid
0.0415	6053.00
0.0888	5965.00
0.1432	5852.00
0.2063	5732.00
0.2806	5538.00
0.3691	5319.00
0.4764	5004.00
0.6094	4546.00
0.7783	3787.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	353.15	20.74
0.0404	353.15	29.88
0.0974	353.15	42.71
0.1972	353.15	61.41
0.2974	353.15	74.25
0.4029	353.15	83.46
0.4980	353.15	88.93
0.5990	353.15	93.05
0.6992	353.15	96.66
0.8004	353.15	100.42
0.8999	353.15	104.33
0.9502	353.15	106.33
1.0000	353.15	108.14
0.0000	363.15	30.23
0.0510	363.15	52.58
0.1005	363.15	70.96
0.2007	363.15	93.42
0.2984	363.15	107.95
0.4039	363.15	120.57
0.4984	363.15	128.93
0.5987	363.15	134.10
0.6987	363.15	138.32
0.8008	363.15	144.58
0.9003	363.15	150.93
0.9504	363.15	153.65
1.0000	363.15	156.04

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	353.15	20.74
0.0404	353.15	29.88
0.0974	353.15	42.71
0.1972	353.15	61.41
0.2974	353.15	74.25
0.4029	353.15	83.46
0.4980	353.15	88.93
0.5990	353.15	93.05
0.6992	353.15	96.66
0.8004	353.15	100.42
0.8999	353.15	104.33
0.9502	353.15	106.33
1.0000	353.15	108.14
0.0000	363.15	30.23
0.0510	363.15	52.58
0.1005	363.15	70.96
0.2007	363.15	93.42
0.2984	363.15	107.95
0.4039	363.15	120.57
0.4984	363.15	128.93
0.5987	363.15	134.10
0.6987	363.15	138.32
0.8008	363.15	144.58
0.9003	363.15	150.93
0.9504	363.15	153.65
1.0000	363.15	156.04

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3594
0.0415	1.3614
0.0943	1.3635
0.1932	1.367
0.2929	1.3698
0.3938	1.3724
0.4965	1.3746
0.5970	1.3765
0.6924	1.3781
0.7911	1.3796
0.8990	1.3811
0.9413	1.3817
1.0000	1.3825

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Diethyl carbonate (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3595
0.0415	1.3614
0.0943	1.3635
0.1932	1.367
0.2929	1.3698
0.3938	1.3724
0.4965	1.3746
0.5970	1.3765
0.6924	1.378
0.7911	1.3796
0.8990	1.3811
0.9413	1.3817
1.0000	1.3825

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3594
0.0415	1.3614
0.0943	1.3635
0.1932	1.367
0.2929	1.3698
0.3938	1.3724
0.4965	1.3746
0.5970	1.3765
0.6924	1.3781
0.7911	1.3796
0.8990	1.3811
0.9413	1.3817
1.0000	1.3825

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Diethyl carbonate (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3595
0.0415	1.3614
0.0943	1.3635
0.1932	1.367
0.2929	1.3698
0.3938	1.3724
0.4965	1.3746
0.5970	1.3765
0.6924	1.378
0.7911	1.3796
0.8990	1.3811
0.9413	1.3817
1.0000	1.3825

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	785.2
0.0415	800.3
0.0943	817.7
0.1932	845.9
0.2929	869.6
0.3938	890.0
0.4965	907.8
0.5970	923.0
0.6924	935.7
0.7911	947.6
0.8990	959.3
0.9413	963.6
1.0000	969.3

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	785.24
0.0415	800.3
0.0943	817.71
0.1932	845.85
0.2929	869.58
0.3938	889.96
0.4965	907.82
0.5970	922.99
0.6924	935.73
0.7911	947.58
0.8990	959.27
0.9413	963.58
1.0000	969.32

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	0.0554	813.88
288.15	0.1000	828.53
288.15	0.1970	856.33
288.15	0.2998	881.02
288.15	0.4062	902.55
288.15	0.5039	919.48
288.15	0.6130	935.91
288.15	0.6939	946.73
288.15	0.7942	958.83
288.15	0.8992	970.29
288.15	0.9744	977.89
293.15	0.0521	808.2
293.15	0.0964	822.76
293.15	0.1983	851.8
293.15	0.2931	874.46
293.15	0.4089	897.78
293.15	0.4945	912.58
293.15	0.6111	930.21
293.15	0.6787	939.26
293.15	0.7692	950.39
293.15	0.8767	962.34
293.15	0.9444	969.33
303.15	0.0459	797.14
303.15	0.0969	813.63
303.15	0.1943	840.98
303.15	0.2843	862.32
303.15	0.4098	887.33
303.15	0.5128	904.7
303.15	0.6176	920.01
303.15	0.6907	929.62
303.15	0.7896	941.46
303.15	0.8863	951.96
303.15	0.9676	960.23
313.15	0.0496	789.32
313.15	0.0965	804.16
313.15	0.2070	834.28
313.15	0.2847	852.21
313.15	0.3982	874.66
313.15	0.5049	892.56
313.15	0.6079	907.66
313.15	0.6227	909.67
313.15	0.6895	918.3
313.15	0.7826	929.4
313.15	0.8924	941.3
313.15	0.9563	947.79

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	785.2
0.0415	800.3
0.0943	817.7
0.1932	845.9
0.2929	869.6
0.3938	890.0
0.4965	907.8
0.5970	923.0
0.6924	935.7
0.7911	947.6
0.8990	959.3
0.9413	963.6
1.0000	969.3

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	785.24
0.0415	800.3
0.0943	817.71
0.1932	845.85
0.2929	869.58
0.3938	889.96
0.4965	907.82
0.5970	922.99
0.6924	935.73
0.7911	947.58
0.8990	959.27
0.9413	963.58
1.0000	969.32

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	0.0554	813.88
288.15	0.1000	828.53
288.15	0.1970	856.33
288.15	0.2998	881.02
288.15	0.4062	902.55
288.15	0.5039	919.48
288.15	0.6130	935.91
288.15	0.6939	946.73
288.15	0.7942	958.83
288.15	0.8992	970.29
288.15	0.9744	977.89
293.15	0.0521	808.2
293.15	0.0964	822.76
293.15	0.1983	851.8
293.15	0.2931	874.46
293.15	0.4089	897.78
293.15	0.4945	912.58
293.15	0.6111	930.21
293.15	0.6787	939.26
293.15	0.7692	950.39
293.15	0.8767	962.34
293.15	0.9444	969.33
303.15	0.0459	797.14
303.15	0.0969	813.63
303.15	0.1943	840.98
303.15	0.2843	862.32
303.15	0.4098	887.33
303.15	0.5128	904.7
303.15	0.6176	920.01
303.15	0.6907	929.62
303.15	0.7896	941.46
303.15	0.8863	951.96
303.15	0.9676	960.23
313.15	0.0496	789.32
313.15	0.0965	804.16
313.15	0.2070	834.28
313.15	0.2847	852.21
313.15	0.3982	874.66
313.15	0.5049	892.56
313.15	0.6079	907.66
313.15	0.6227	909.67
313.15	0.6895	918.3
313.15	0.7826	929.4
313.15	0.8924	941.3
313.15	0.9563	947.79

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Speed of sound, m/s - Liquid
0.0000	1142.0
0.0415	1145.0
0.0943	1147.0
0.1932	1150.0
0.2929	1154.0
0.3938	1156.0
0.4965	1159.0
0.5970	1162.0
0.6924	1166.0
0.7911	1169.0
0.8990	1173.0
0.9413	1175.0
1.0000	1177.0

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)
• Frequency, MHz = 3 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Speed of sound, m/s - Liquid
0.0000	1142.8
0.0415	1145.2
0.0943	1147.3
0.1932	1150.9
0.2929	1154.0
0.3938	1156.9
0.4965	1159.8
0.5970	1162.8
0.6924	1166.0
0.7911	1169.7
0.8990	1173.7
0.9413	1175.0
1.0000	1176.6

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Speed of sound, m/s - Liquid
0.0000	1142.0
0.0415	1145.0
0.0943	1147.0
0.1932	1150.0
0.2929	1154.0
0.3938	1156.0
0.4965	1159.0
0.5970	1162.0
0.6924	1166.0
0.7911	1169.0
0.8990	1173.0
0.9413	1175.0
1.0000	1177.0

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)
• Frequency, MHz = 3 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Speed of sound, m/s - Liquid
0.0000	1142.8
0.0415	1145.2
0.0943	1147.3
0.1932	1150.9
0.2929	1154.0
0.3938	1156.9
0.4965	1159.8
0.5970	1162.8
0.6924	1166.0
0.7911	1169.7
0.8990	1173.7
0.9413	1175.0
1.0000	1176.6

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0157	396.02
0.0315	392.45
0.0464	389.31
0.0671	385.53
0.0851	382.53
0.1061	379.44
0.1341	375.88
0.1615	372.96
0.1951	370.00
0.2195	368.25
0.2472	366.50
0.2725	365.20
0.3070	363.65
0.3425	362.36
0.3796	361.24
0.4168	360.27
0.4524	359.45
0.4836	358.73
0.5018	358.45
0.5395	357.67
0.5633	357.25
0.6074	356.47
0.6464	355.82
0.6905	355.12
0.7282	354.57
0.7895	353.78
0.8222	353.46
0.8528	353.15
0.8828	352.84
0.9112	352.50
0.9331	352.32
0.9541	352.10
0.9649	351.91
0.9861	351.73

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0157	396.02
0.0315	392.45
0.0464	389.31
0.0671	385.53
0.0851	382.53
0.1061	379.44
0.1341	375.88
0.1615	372.96
0.1951	370.00
0.2195	368.25
0.2472	366.50
0.2725	365.20
0.3070	363.65
0.3425	362.36
0.3796	361.24
0.4168	360.27
0.4524	359.45
0.4836	358.73
0.5018	358.45
0.5395	357.67
0.5633	357.25
0.6074	356.47
0.6464	355.82
0.6905	355.12
0.7282	354.57
0.7895	353.78
0.8222	353.46
0.8528	353.15
0.8828	352.84
0.9112	352.50
0.9331	352.32
0.9541	352.10
0.9649	351.91
0.9861	351.73

Critical temperature, K [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical temperature, K - Liquid
0.0415	519.00
0.0888	522.30
0.1432	526.90
0.2063	531.00
0.2806	537.10
0.3691	541.70
0.4764	547.30
0.6094	555.30
0.7783	566.50

Critical temperature, K [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical temperature, K - Liquid
0.0415	519.00
0.0888	522.30
0.1432	526.90
0.2063	531.00
0.2806	537.10
0.3691	541.70
0.4764	547.30
0.6094	555.30
0.7783	566.50

Sources

• Isothermal vapor liquid and vapor liquid liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
• Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
• Effect of temperature on density, sound velocity, refractive index and their derived properties for the binary systems (heptanoic acid + propanoic or butanoic acids)
• Influence of alkyl group and temperature on thermophysical properties of carboxylic acid and their binary mixtures
• 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
• Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K