Mixture of Diethyl carbonate + Ethanol

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Diethyl carbonate

Name
Diethyl carbonate
InChI
InChI=1S/C5H10O3/c1-3-7-5(6)8-4-2/h3-4H2,1-2H3
InChI Key
OIFBSDVPJOWBCH-UHFFFAOYSA-N
Formula
C5H10O3
SMILES
CCOC(=O)OCC
Mol. Weight (g/mol)
118.13
CAS
105-58-8

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5
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Datasets

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

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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