Mixture of Diethyl carbonate + 1-Butanol

Excel

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

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (4)
  3. ρl - Mass density, kg/m3 (2)
  4. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of 1-Butanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Mole fraction of 1-Butanol (2) - Gas
0.0135 0.0239
0.0409 0.0715
0.0682 0.1170
0.0910 0.1535
0.1277 0.2056
0.1498 0.2357
0.1844 0.2809
0.2033 0.3028
0.2537 0.3589
0.3038 0.4114
0.3502 0.4547
0.3807 0.4827
0.4250 0.5184
0.4519 0.5407
0.4835 0.5657
0.5065 0.5797
0.5422 0.6035
0.5767 0.6294
0.6047 0.6480
0.6411 0.6717
0.6837 0.6967
0.7136 0.7212
0.7542 0.7465
0.7930 0.7762
0.8316 0.8081
0.8784 0.8521
0.9043 0.8784
0.9314 0.9079
0.9632 0.9466
0.9901 0.9846

Mole fraction of 1-Butanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Mole fraction of 1-Butanol (2) - Gas
0.0135 0.0239
0.0409 0.0715
0.0682 0.1170
0.0910 0.1535
0.1277 0.2056
0.1498 0.2357
0.1844 0.2809
0.2033 0.3028
0.2537 0.3589
0.3038 0.4114
0.3502 0.4547
0.3807 0.4827
0.4250 0.5184
0.4519 0.5407
0.4835 0.5657
0.5065 0.5797
0.5422 0.6035
0.5767 0.6294
0.6047 0.6480
0.6411 0.6717
0.6837 0.6967
0.7136 0.7212
0.7542 0.7465
0.7930 0.7762
0.8316 0.8081
0.8784 0.8521
0.9043 0.8784
0.9314 0.9079
0.9632 0.9466
0.9901 0.9846

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 0.0029
293.15 0.0510 0.0025
293.15 0.1027 0.0021
293.15 0.2008 0.0017
293.15 0.2978 0.0014
293.15 0.4026 0.0012
293.15 0.5079 0.0010
293.15 0.6014 0.0009
293.15 0.7033 0.0009
293.15 0.7986 0.0008
293.15 0.9031 0.0008
293.15 0.9510 0.0008
293.15 1.0000 0.0008
298.15 0.0000 0.0026
298.15 0.0519 0.0022
298.15 0.0993 0.0019
298.15 0.1996 0.0014
298.15 0.2923 0.0012
298.15 0.3989 0.0010
298.15 0.5017 0.0009
298.15 0.6016 0.0009
298.15 0.7043 0.0008
298.15 0.8002 0.0008
298.15 0.8968 0.0007
298.15 0.9471 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0023
303.15 0.0508 0.0019
303.15 0.1004 0.0016
303.15 0.2016 0.0013
303.15 0.3000 0.0011
303.15 0.3917 0.0010
303.15 0.5032 0.0009
303.15 0.5970 0.0008
303.15 0.7099 0.0007
303.15 0.8216 0.0007
303.15 0.9035 0.0007
303.15 0.9488 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0018
313.15 0.0506 0.0015
313.15 0.1007 0.0014
313.15 0.2005 0.0011
313.15 0.2975 0.0009
313.15 0.4122 0.0008
313.15 0.5035 0.0007
313.15 0.6084 0.0007
313.15 0.7044 0.0007
313.15 0.8055 0.0006
313.15 0.9016 0.0006
313.15 0.9486 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 0.0022
293.15 0.2023 0.0017
293.15 0.2974 0.0014
298.15 0.1016 0.0019
298.15 0.2023 0.0015
298.15 0.2974 0.0013
303.15 0.1016 0.0017
303.15 0.2023 0.0013
303.15 0.2974 0.0011
313.15 0.1016 0.0013
313.15 0.2023 0.0011
313.15 0.2974 0.0009
323.15 0.1016 0.0011
323.15 0.2023 0.0009
323.15 0.2974 0.0008
333.15 0.1016 0.0009
333.15 0.2023 0.0008
333.15 0.2974 0.0007
343.15 0.1016 0.0007
343.15 0.2023 0.0006
343.15 0.2974 0.0006
353.15 0.1016 0.0006
353.15 0.2023 0.0005
353.15 0.2974 0.0005
363.15 0.1016 0.0005
363.15 0.2023 0.0005
363.15 0.2974 0.0004

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 0.0029
293.15 0.0510 0.0025
293.15 0.1027 0.0021
293.15 0.2008 0.0017
293.15 0.2978 0.0014
293.15 0.4026 0.0012
293.15 0.5079 0.0010
293.15 0.6014 0.0009
293.15 0.7033 0.0009
293.15 0.7986 0.0008
293.15 0.9031 0.0008
293.15 0.9510 0.0008
293.15 1.0000 0.0008
298.15 0.0000 0.0026
298.15 0.0519 0.0022
298.15 0.0993 0.0019
298.15 0.1996 0.0014
298.15 0.2923 0.0012
298.15 0.3989 0.0010
298.15 0.5017 0.0009
298.15 0.6016 0.0009
298.15 0.7043 0.0008
298.15 0.8002 0.0008
298.15 0.8968 0.0007
298.15 0.9471 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0023
303.15 0.0508 0.0019
303.15 0.1004 0.0016
303.15 0.2016 0.0013
303.15 0.3000 0.0011
303.15 0.3917 0.0010
303.15 0.5032 0.0009
303.15 0.5970 0.0008
303.15 0.7099 0.0007
303.15 0.8216 0.0007
303.15 0.9035 0.0007
303.15 0.9488 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0018
313.15 0.0506 0.0015
313.15 0.1007 0.0014
313.15 0.2005 0.0011
313.15 0.2975 0.0009
313.15 0.4122 0.0008
313.15 0.5035 0.0007
313.15 0.6084 0.0007
313.15 0.7044 0.0007
313.15 0.8055 0.0006
313.15 0.9016 0.0006
313.15 0.9486 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 0.0022
293.15 0.2023 0.0017
293.15 0.2974 0.0014
298.15 0.1016 0.0019
298.15 0.2023 0.0015
298.15 0.2974 0.0013
303.15 0.1016 0.0017
303.15 0.2023 0.0013
303.15 0.2974 0.0011
313.15 0.1016 0.0013
313.15 0.2023 0.0011
313.15 0.2974 0.0009
323.15 0.1016 0.0011
323.15 0.2023 0.0009
323.15 0.2974 0.0008
333.15 0.1016 0.0009
333.15 0.2023 0.0008
333.15 0.2974 0.0007
343.15 0.1016 0.0007
343.15 0.2023 0.0006
343.15 0.2974 0.0006
353.15 0.1016 0.0006
353.15 0.2023 0.0005
353.15 0.2974 0.0005
363.15 0.1016 0.0005
363.15 0.2023 0.0005
363.15 0.2974 0.0004

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 830.56
293.15 0.2023 849.89
293.15 0.2974 867.23
298.15 0.1016 826.34
298.15 0.2023 845.4
298.15 0.2974 862.6
303.15 0.1016 821.75
303.15 0.2023 840.53
303.15 0.2974 857.48
313.15 0.1016 812.55
313.15 0.2023 831.22
313.15 0.2974 847.88
323.15 0.1016 804.95
323.15 0.2023 822.83
323.15 0.2974 838.91
333.15 0.1016 795.85
333.15 0.2023 813.37
333.15 0.2974 829.07
343.15 0.1016 784.94
343.15 0.2023 802.09
343.15 0.2974 817.6
353.15 0.1016 775.15
353.15 0.2023 792.01
353.15 0.2974 807.21
363.15 0.1016 766.42
363.15 0.2023 782.78
363.15 0.2974 797.61

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 830.56
293.15 0.2023 849.89
293.15 0.2974 867.23
298.15 0.1016 826.34
298.15 0.2023 845.4
298.15 0.2974 862.6
303.15 0.1016 821.75
303.15 0.2023 840.53
303.15 0.2974 857.48
313.15 0.1016 812.55
313.15 0.2023 831.22
313.15 0.2974 847.88
323.15 0.1016 804.95
323.15 0.2023 822.83
323.15 0.2974 838.91
333.15 0.1016 795.85
333.15 0.2023 813.37
333.15 0.2974 829.07
343.15 0.1016 784.94
343.15 0.2023 802.09
343.15 0.2974 817.6
353.15 0.1016 775.15
353.15 0.2023 792.01
353.15 0.2974 807.21
363.15 0.1016 766.42
363.15 0.2023 782.78
363.15 0.2974 797.61

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0135 398.97
0.0409 398.17
0.0682 397.20
0.0910 396.45
0.1277 395.45
0.1498 394.86
0.1844 394.14
0.2033 393.73
0.2537 392.88
0.3038 392.15
0.3502 391.59
0.3807 391.30
0.4250 390.87
0.4519 390.59
0.4835 390.35
0.5065 390.24
0.5422 390.03
0.5767 389.88
0.6047 389.73
0.6411 389.60
0.6837 389.52
0.7136 389.48
0.7542 389.47
0.7930 389.52
0.8316 389.67
0.8784 389.85
0.9043 390.05
0.9314 390.22
0.9632 390.50
0.9901 390.77

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0135 398.97
0.0409 398.17
0.0682 397.20
0.0910 396.45
0.1277 395.45
0.1498 394.86
0.1844 394.14
0.2033 393.73
0.2537 392.88
0.3038 392.15
0.3502 391.59
0.3807 391.30
0.4250 390.87
0.4519 390.59
0.4835 390.35
0.5065 390.24
0.5422 390.03
0.5767 389.88
0.6047 389.73
0.6411 389.60
0.6837 389.52
0.7136 389.48
0.7542 389.47
0.7930 389.52
0.8316 389.67
0.8784 389.85
0.9043 390.05
0.9314 390.22
0.9632 390.50
0.9901 390.77

Sources