Mixture of Diethyl carbonate + Isopropyl Alcohol

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

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0
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Datasets

  1. η - Viscosity, Pa*s (4)
  2. ρl - Mass density, kg/m3 (2)

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 0.0024
293.15 0.0502 0.0020
293.15 0.1001 0.0017
293.15 0.2030 0.0013
293.15 0.3012 0.0011
293.15 0.3954 0.0010
293.15 0.5021 0.0009
293.15 0.6035 0.0008
293.15 0.6976 0.0008
293.15 0.8048 0.0008
293.15 0.9129 0.0008
293.15 0.9529 0.0008
293.15 1.0000 0.0008
298.15 0.0000 0.0021
298.15 0.0490 0.0018
298.15 0.0987 0.0015
298.15 0.1978 0.0011
298.15 0.2945 0.0009
298.15 0.3925 0.0008
298.15 0.4925 0.0008
298.15 0.5939 0.0008
298.15 0.7004 0.0007
298.15 0.7979 0.0007
298.15 0.8967 0.0007
298.15 0.9504 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0018
303.15 0.0522 0.0015
303.15 0.0990 0.0013
303.15 0.1944 0.0010
303.15 0.2913 0.0009
303.15 0.3920 0.0008
303.15 0.4763 0.0007
303.15 0.5883 0.0007
303.15 0.6972 0.0007
303.15 0.7854 0.0007
303.15 0.8890 0.0007
303.15 0.9488 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0013
313.15 0.0506 0.0011
313.15 0.0997 0.0010
313.15 0.2016 0.0008
313.15 0.3030 0.0007
313.15 0.4008 0.0007
313.15 0.4969 0.0006
313.15 0.5990 0.0006
313.15 0.7007 0.0006
313.15 0.8011 0.0006
313.15 0.9030 0.0006
313.15 0.9511 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 0.0000 0.0024
293.15 0.1015 0.0016
293.15 0.1993 0.0013
293.15 0.3027 0.0011
293.15 0.4029 0.0009
293.15 0.5018 0.0009
293.15 0.5905 0.0008
293.15 0.7267 0.0008
293.15 0.8053 0.0008
293.15 0.8494 0.0008
293.15 1.0000 0.0008
298.15 0.0000 0.0021
298.15 0.1015 0.0014
298.15 0.1993 0.0011
298.15 0.3027 0.0010
298.15 0.4029 0.0009
298.15 0.5018 0.0008
298.15 0.5905 0.0008
298.15 0.7267 0.0007
298.15 0.8053 0.0007
298.15 0.8494 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0017
303.15 0.1015 0.0012
303.15 0.1993 0.0010
303.15 0.3027 0.0009
303.15 0.4029 0.0008
303.15 0.5018 0.0007
303.15 0.5905 0.0007
303.15 0.7267 0.0007
303.15 0.8053 0.0007
303.15 0.8494 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0013
313.15 0.1015 0.0010
313.15 0.1993 0.0008
313.15 0.3027 0.0007
313.15 0.4029 0.0007
313.15 0.5018 0.0006
313.15 0.5905 0.0006
313.15 0.7267 0.0006
313.15 0.8053 0.0006
313.15 0.8494 0.0006
313.15 1.0000 0.0006
323.15 0.0000 0.0010
323.15 0.1015 0.0008
323.15 0.1993 0.0007
323.15 0.3027 0.0006
323.15 0.4029 0.0006
323.15 0.5018 0.0005
323.15 0.5905 0.0005
323.15 0.7267 0.0005
323.15 0.8053 0.0005
323.15 0.8494 0.0005
323.15 1.0000 0.0005
333.15 0.0000 0.0008
333.15 0.1015 0.0006
333.15 0.1993 0.0006
333.15 0.3027 0.0005
333.15 0.4029 0.0005
333.15 0.5018 0.0005
333.15 0.5905 0.0005
333.15 0.7267 0.0005
333.15 0.8053 0.0005
333.15 0.8494 0.0005
333.15 1.0000 0.0005
343.15 0.0000 0.0006
343.15 0.1015 0.0005
343.15 0.1993 0.0005
343.15 0.3027 0.0004
343.15 0.4029 0.0004
343.15 0.5018 0.0004
343.15 0.5905 0.0004
343.15 0.7267 0.0004
343.15 0.8053 0.0004
343.15 0.8494 0.0004
343.15 1.0000 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 0.0024
293.15 0.0502 0.0020
293.15 0.1001 0.0017
293.15 0.2030 0.0013
293.15 0.3012 0.0011
293.15 0.3954 0.0010
293.15 0.5021 0.0009
293.15 0.6035 0.0008
293.15 0.6976 0.0008
293.15 0.8048 0.0008
293.15 0.9129 0.0008
293.15 0.9529 0.0008
293.15 1.0000 0.0008
298.15 0.0000 0.0021
298.15 0.0490 0.0018
298.15 0.0987 0.0015
298.15 0.1978 0.0011
298.15 0.2945 0.0009
298.15 0.3925 0.0008
298.15 0.4925 0.0008
298.15 0.5939 0.0008
298.15 0.7004 0.0007
298.15 0.7979 0.0007
298.15 0.8967 0.0007
298.15 0.9504 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0018
303.15 0.0522 0.0015
303.15 0.0990 0.0013
303.15 0.1944 0.0010
303.15 0.2913 0.0009
303.15 0.3920 0.0008
303.15 0.4763 0.0007
303.15 0.5883 0.0007
303.15 0.6972 0.0007
303.15 0.7854 0.0007
303.15 0.8890 0.0007
303.15 0.9488 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0013
313.15 0.0506 0.0011
313.15 0.0997 0.0010
313.15 0.2016 0.0008
313.15 0.3030 0.0007
313.15 0.4008 0.0007
313.15 0.4969 0.0006
313.15 0.5990 0.0006
313.15 0.7007 0.0006
313.15 0.8011 0.0006
313.15 0.9030 0.0006
313.15 0.9511 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 0.0000 0.0024
293.15 0.1015 0.0016
293.15 0.1993 0.0013
293.15 0.3027 0.0011
293.15 0.4029 0.0009
293.15 0.5018 0.0009
293.15 0.5905 0.0008
293.15 0.7267 0.0008
293.15 0.8053 0.0008
293.15 0.8494 0.0008
293.15 1.0000 0.0008
298.15 0.0000 0.0021
298.15 0.1015 0.0014
298.15 0.1993 0.0011
298.15 0.3027 0.0010
298.15 0.4029 0.0009
298.15 0.5018 0.0008
298.15 0.5905 0.0008
298.15 0.7267 0.0007
298.15 0.8053 0.0007
298.15 0.8494 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0017
303.15 0.1015 0.0012
303.15 0.1993 0.0010
303.15 0.3027 0.0009
303.15 0.4029 0.0008
303.15 0.5018 0.0007
303.15 0.5905 0.0007
303.15 0.7267 0.0007
303.15 0.8053 0.0007
303.15 0.8494 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0013
313.15 0.1015 0.0010
313.15 0.1993 0.0008
313.15 0.3027 0.0007
313.15 0.4029 0.0007
313.15 0.5018 0.0006
313.15 0.5905 0.0006
313.15 0.7267 0.0006
313.15 0.8053 0.0006
313.15 0.8494 0.0006
313.15 1.0000 0.0006
323.15 0.0000 0.0010
323.15 0.1015 0.0008
323.15 0.1993 0.0007
323.15 0.3027 0.0006
323.15 0.4029 0.0006
323.15 0.5018 0.0005
323.15 0.5905 0.0005
323.15 0.7267 0.0005
323.15 0.8053 0.0005
323.15 0.8494 0.0005
323.15 1.0000 0.0005
333.15 0.0000 0.0008
333.15 0.1015 0.0006
333.15 0.1993 0.0006
333.15 0.3027 0.0005
333.15 0.4029 0.0005
333.15 0.5018 0.0005
333.15 0.5905 0.0005
333.15 0.7267 0.0005
333.15 0.8053 0.0005
333.15 0.8494 0.0005
333.15 1.0000 0.0005
343.15 0.0000 0.0006
343.15 0.1015 0.0005
343.15 0.1993 0.0005
343.15 0.3027 0.0004
343.15 0.4029 0.0004
343.15 0.5018 0.0004
343.15 0.5905 0.0004
343.15 0.7267 0.0004
343.15 0.8053 0.0004
343.15 0.8494 0.0004
343.15 1.0000 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 0.0000 785.28
293.15 0.1015 812.95
293.15 0.1993 837.12
293.15 0.3027 861.52
293.15 0.4029 880.88
293.15 0.5018 901.57
293.15 0.5905 914.48
293.15 0.7267 936.22
293.15 0.8053 947.93
293.15 0.8494 954.32
293.15 1.0000 975.0
298.15 0.0000 780.69
298.15 0.1015 808.12
298.15 0.1993 831.98
298.15 0.3027 855.03
298.15 0.4029 875.34
298.15 0.5018 893.55
298.15 0.5905 908.68
298.15 0.7267 930.3
298.15 0.8053 941.94
298.15 0.8494 948.31
298.15 1.0000 968.97
303.15 0.0000 776.15
303.15 0.1015 803.27
303.15 0.1993 826.84
303.15 0.3027 849.57
303.15 0.4029 869.48
303.15 0.5018 887.62
303.15 0.5905 902.71
303.15 0.7267 924.09
303.15 0.8053 935.6
303.15 0.8494 941.89
303.15 1.0000 962.39
313.15 0.0000 766.34
313.15 0.1015 793.12
313.15 0.1993 816.46
313.15 0.3027 839.13
313.15 0.4029 859.2
313.15 0.5018 877.18
313.15 0.5905 892.18
313.15 0.7267 913.63
313.15 0.8053 925.25
313.15 0.8494 931.59
313.15 1.0000 952.32
323.15 0.0000 755.66
323.15 0.1015 781.71
323.15 0.1993 804.58
323.15 0.3027 826.95
323.15 0.4029 846.73
323.15 0.5018 864.62
323.15 0.5905 879.49
323.15 0.7267 900.94
323.15 0.8053 912.58
323.15 0.8494 918.93
323.15 1.0000 939.78
333.15 0.0000 745.51
333.15 0.1015 771.12
333.15 0.1993 793.64
333.15 0.3027 815.77
333.15 0.4029 835.41
333.15 0.5018 853.29
333.15 0.5905 868.1
333.15 0.7267 889.56
333.15 0.8053 901.29
333.15 0.8494 907.67
333.15 1.0000 928.69
343.15 0.0000 735.02
343.15 0.1015 760.13
343.15 0.1993 782.3
343.15 0.3027 804.17
343.15 0.4029 823.53
343.15 0.5018 841.14
343.15 0.5905 855.92
343.15 0.7267 877.3
343.15 0.8053 888.96
343.15 0.8494 895.36
343.15 1.0000 916.33

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 0.0000 785.28
293.15 0.1015 812.95
293.15 0.1993 837.12
293.15 0.3027 861.52
293.15 0.4029 880.88
293.15 0.5018 901.57
293.15 0.5905 914.48
293.15 0.7267 936.22
293.15 0.8053 947.93
293.15 0.8494 954.32
293.15 1.0000 975.0
298.15 0.0000 780.69
298.15 0.1015 808.12
298.15 0.1993 831.98
298.15 0.3027 855.03
298.15 0.4029 875.34
298.15 0.5018 893.55
298.15 0.5905 908.68
298.15 0.7267 930.3
298.15 0.8053 941.94
298.15 0.8494 948.31
298.15 1.0000 968.97
303.15 0.0000 776.15
303.15 0.1015 803.27
303.15 0.1993 826.84
303.15 0.3027 849.57
303.15 0.4029 869.48
303.15 0.5018 887.62
303.15 0.5905 902.71
303.15 0.7267 924.09
303.15 0.8053 935.6
303.15 0.8494 941.89
303.15 1.0000 962.39
313.15 0.0000 766.34
313.15 0.1015 793.12
313.15 0.1993 816.46
313.15 0.3027 839.13
313.15 0.4029 859.2
313.15 0.5018 877.18
313.15 0.5905 892.18
313.15 0.7267 913.63
313.15 0.8053 925.25
313.15 0.8494 931.59
313.15 1.0000 952.32
323.15 0.0000 755.66
323.15 0.1015 781.71
323.15 0.1993 804.58
323.15 0.3027 826.95
323.15 0.4029 846.73
323.15 0.5018 864.62
323.15 0.5905 879.49
323.15 0.7267 900.94
323.15 0.8053 912.58
323.15 0.8494 918.93
323.15 1.0000 939.78
333.15 0.0000 745.51
333.15 0.1015 771.12
333.15 0.1993 793.64
333.15 0.3027 815.77
333.15 0.4029 835.41
333.15 0.5018 853.29
333.15 0.5905 868.1
333.15 0.7267 889.56
333.15 0.8053 901.29
333.15 0.8494 907.67
333.15 1.0000 928.69
343.15 0.0000 735.02
343.15 0.1015 760.13
343.15 0.1993 782.3
343.15 0.3027 804.17
343.15 0.4029 823.53
343.15 0.5018 841.14
343.15 0.5905 855.92
343.15 0.7267 877.3
343.15 0.8053 888.96
343.15 0.8494 895.36
343.15 1.0000 916.33

Sources