Mixture of 1-Propanol + Butanedioic acid, diethyl ester

Excel

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

Butanedioic acid, diethyl ester

Name
Butanedioic acid, diethyl ester
InChI
InChI=1S/C8H14O4/c1-3-11-7(9)5-6-8(10)12-4-2/h3-6H2,1-2H3
InChI Key
DKMROQRQHGEIOW-UHFFFAOYSA-N
Formula
C8H14O4
SMILES
CCOC(=O)CCC(=O)OCC
Mol. Weight (g/mol)
174.19
CAS
123-25-1
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. n0 - Refractive index (Na D-line) (2)
  3. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid Viscosity, Pa*s - Liquid
288.15 0.0000 0.0025
288.15 0.1000 0.0021
288.15 0.2000 0.0020
288.15 0.2999 0.0020
288.15 0.3998 0.0021
288.15 0.4999 0.0022
288.15 0.6001 0.0023
288.15 0.7001 0.0025
288.15 0.8002 0.0027
288.15 0.8997 0.0029
288.15 1.0000 0.0032
293.15 0.0000 0.0022
293.15 0.1000 0.0019
293.15 0.2000 0.0018
293.15 0.2999 0.0018
293.15 0.3998 0.0019
293.15 0.4999 0.0020
293.15 0.6001 0.0021
293.15 0.7001 0.0022
293.15 0.8002 0.0024
293.15 0.8997 0.0026
293.15 1.0000 0.0028
298.15 0.0000 0.0020
298.15 0.1000 0.0017
298.15 0.2000 0.0016
298.15 0.2999 0.0016
298.15 0.3998 0.0017
298.15 0.4999 0.0018
298.15 0.6001 0.0019
298.15 0.7001 0.0020
298.15 0.8002 0.0021
298.15 0.8997 0.0023
298.15 1.0000 0.0025
303.15 0.0000 0.0017
303.15 0.1000 0.0015
303.15 0.2000 0.0015
303.15 0.2999 0.0015
303.15 0.3998 0.0015
303.15 0.4999 0.0016
303.15 0.6001 0.0017
303.15 0.7001 0.0018
303.15 0.8002 0.0019
303.15 0.8997 0.0021
303.15 1.0000 0.0022
308.15 0.0000 0.0015
308.15 0.1000 0.0014
308.15 0.2000 0.0013
308.15 0.2999 0.0013
308.15 0.3998 0.0014
308.15 0.4999 0.0014
308.15 0.6001 0.0015
308.15 0.7001 0.0016
308.15 0.8002 0.0017
308.15 0.8997 0.0019
308.15 1.0000 0.0020
313.15 0.0000 0.0014
313.15 0.1000 0.0012
313.15 0.2000 0.0012
313.15 0.2999 0.0012
313.15 0.3998 0.0013
313.15 0.4999 0.0013
313.15 0.6001 0.0014
313.15 0.7001 0.0015
313.15 0.8002 0.0016
313.15 0.8997 0.0017
313.15 1.0000 0.0018
318.15 0.0000 0.0012
318.15 0.1000 0.0011
318.15 0.2000 0.0011
318.15 0.2999 0.0011
318.15 0.3998 0.0011
318.15 0.4999 0.0012
318.15 0.6001 0.0013
318.15 0.7001 0.0014
318.15 0.8002 0.0014
318.15 0.8997 0.0015
318.15 1.0000 0.0017
323.15 0.0000 0.0011
323.15 0.1000 0.0010
323.15 0.2000 0.0010
323.15 0.2999 0.0010
323.15 0.3998 0.0011
323.15 0.4999 0.0011
323.15 0.6001 0.0012
323.15 0.7001 0.0013
323.15 0.8002 0.0013
323.15 0.8997 0.0014
323.15 1.0000 0.0015

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid Viscosity, Pa*s - Liquid
288.15 0.0000 0.0025
288.15 0.1000 0.0021
288.15 0.2000 0.0020
288.15 0.2999 0.0020
288.15 0.3998 0.0021
288.15 0.4999 0.0022
288.15 0.6001 0.0023
288.15 0.7001 0.0025
288.15 0.8002 0.0027
288.15 0.8997 0.0029
288.15 1.0000 0.0032
293.15 0.0000 0.0022
293.15 0.1000 0.0019
293.15 0.2000 0.0018
293.15 0.2999 0.0018
293.15 0.3998 0.0019
293.15 0.4999 0.0020
293.15 0.6001 0.0021
293.15 0.7001 0.0022
293.15 0.8002 0.0024
293.15 0.8997 0.0026
293.15 1.0000 0.0028
298.15 0.0000 0.0020
298.15 0.1000 0.0017
298.15 0.2000 0.0016
298.15 0.2999 0.0016
298.15 0.3998 0.0017
298.15 0.4999 0.0018
298.15 0.6001 0.0019
298.15 0.7001 0.0020
298.15 0.8002 0.0021
298.15 0.8997 0.0023
298.15 1.0000 0.0025
303.15 0.0000 0.0017
303.15 0.1000 0.0015
303.15 0.2000 0.0015
303.15 0.2999 0.0015
303.15 0.3998 0.0015
303.15 0.4999 0.0016
303.15 0.6001 0.0017
303.15 0.7001 0.0018
303.15 0.8002 0.0019
303.15 0.8997 0.0021
303.15 1.0000 0.0022
308.15 0.0000 0.0015
308.15 0.1000 0.0014
308.15 0.2000 0.0013
308.15 0.2999 0.0013
308.15 0.3998 0.0014
308.15 0.4999 0.0014
308.15 0.6001 0.0015
308.15 0.7001 0.0016
308.15 0.8002 0.0017
308.15 0.8997 0.0019
308.15 1.0000 0.0020
313.15 0.0000 0.0014
313.15 0.1000 0.0012
313.15 0.2000 0.0012
313.15 0.2999 0.0012
313.15 0.3998 0.0013
313.15 0.4999 0.0013
313.15 0.6001 0.0014
313.15 0.7001 0.0015
313.15 0.8002 0.0016
313.15 0.8997 0.0017
313.15 1.0000 0.0018
318.15 0.0000 0.0012
318.15 0.1000 0.0011
318.15 0.2000 0.0011
318.15 0.2999 0.0011
318.15 0.3998 0.0011
318.15 0.4999 0.0012
318.15 0.6001 0.0013
318.15 0.7001 0.0014
318.15 0.8002 0.0014
318.15 0.8997 0.0015
318.15 1.0000 0.0017
323.15 0.0000 0.0011
323.15 0.1000 0.0010
323.15 0.2000 0.0010
323.15 0.2999 0.0010
323.15 0.3998 0.0011
323.15 0.4999 0.0011
323.15 0.6001 0.0012
323.15 0.7001 0.0013
323.15 0.8002 0.0013
323.15 0.8997 0.0014
323.15 1.0000 0.0015

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid Refractive index (Na D-line) - Liquid
288.15 0.0000 1.3875
288.15 0.1000 1.394
288.15 0.2000 1.3993
288.15 0.2999 1.4037
288.15 0.3998 1.4075
288.15 0.4999 1.4107
288.15 0.6001 1.4135
288.15 0.7001 1.416
288.15 0.8002 1.4182
288.15 0.8997 1.4201
288.15 1.0000 1.4217
293.15 0.0000 1.3854
293.15 0.1000 1.3918
293.15 0.2000 1.3971
293.15 0.2999 1.4016
293.15 0.3998 1.4053
293.15 0.4999 1.4085
293.15 0.6001 1.4113
293.15 0.7001 1.4138
293.15 0.8002 1.416
293.15 0.8997 1.4179
293.15 1.0000 1.4195
298.15 0.0000 1.3834
298.15 0.1000 1.3897
298.15 0.2000 1.395
298.15 0.2999 1.3994
298.15 0.3998 1.4031
298.15 0.4999 1.4063
298.15 0.6001 1.4091
298.15 0.7001 1.4116
298.15 0.8002 1.4138
298.15 0.8997 1.4157
298.15 1.0000 1.4173
303.15 0.0000 1.3814
303.15 0.1000 1.3876
303.15 0.2000 1.3928
303.15 0.2999 1.3972
303.15 0.3998 1.4009
303.15 0.4999 1.4041
303.15 0.6001 1.4069
303.15 0.7001 1.4094
303.15 0.8002 1.4116
303.15 0.8997 1.4135
303.15 1.0000 1.4151
308.15 0.0000 1.3792
308.15 0.1000 1.3854
308.15 0.2000 1.3906
308.15 0.2999 1.3949
308.15 0.3998 1.3986
308.15 0.4999 1.4018
308.15 0.6001 1.4047
308.15 0.7001 1.4072
308.15 0.8002 1.4094
308.15 0.8997 1.4113
308.15 1.0000 1.4129
313.15 0.0000 1.377
313.15 0.1000 1.3831
313.15 0.2000 1.3883
313.15 0.2999 1.3927
313.15 0.3998 1.3964
313.15 0.4999 1.3996
313.15 0.6001 1.4025
313.15 0.7001 1.4049
313.15 0.8002 1.4072
313.15 0.8997 1.4091
313.15 1.0000 1.4108
318.15 0.0000 1.3748
318.15 0.1000 1.3809
318.15 0.2000 1.3861
318.15 0.2999 1.3905
318.15 0.3998 1.3942
318.15 0.4999 1.3974
318.15 0.6001 1.4002
318.15 0.7001 1.4027
318.15 0.8002 1.4049
318.15 0.8997 1.4069
318.15 1.0000 1.4088
323.15 0.0000 1.3726
323.15 0.1000 1.3787
323.15 0.2000 1.3839
323.15 0.2999 1.3882
323.15 0.3998 1.392
323.15 0.4999 1.3952
323.15 0.6001 1.398
323.15 0.7001 1.4005
323.15 0.8002 1.4027
323.15 0.8997 1.4048
323.15 1.0000 1.4067

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid Refractive index (Na D-line) - Liquid
288.15 0.0000 1.3875
288.15 0.1000 1.394
288.15 0.2000 1.3993
288.15 0.2999 1.4037
288.15 0.3998 1.4075
288.15 0.4999 1.4107
288.15 0.6001 1.4135
288.15 0.7001 1.416
288.15 0.8002 1.4182
288.15 0.8997 1.4201
288.15 1.0000 1.4217
293.15 0.0000 1.3854
293.15 0.1000 1.3918
293.15 0.2000 1.3971
293.15 0.2999 1.4016
293.15 0.3998 1.4053
293.15 0.4999 1.4085
293.15 0.6001 1.4113
293.15 0.7001 1.4138
293.15 0.8002 1.416
293.15 0.8997 1.4179
293.15 1.0000 1.4195
298.15 0.0000 1.3834
298.15 0.1000 1.3897
298.15 0.2000 1.395
298.15 0.2999 1.3994
298.15 0.3998 1.4031
298.15 0.4999 1.4063
298.15 0.6001 1.4091
298.15 0.7001 1.4116
298.15 0.8002 1.4138
298.15 0.8997 1.4157
298.15 1.0000 1.4173
303.15 0.0000 1.3814
303.15 0.1000 1.3876
303.15 0.2000 1.3928
303.15 0.2999 1.3972
303.15 0.3998 1.4009
303.15 0.4999 1.4041
303.15 0.6001 1.4069
303.15 0.7001 1.4094
303.15 0.8002 1.4116
303.15 0.8997 1.4135
303.15 1.0000 1.4151
308.15 0.0000 1.3792
308.15 0.1000 1.3854
308.15 0.2000 1.3906
308.15 0.2999 1.3949
308.15 0.3998 1.3986
308.15 0.4999 1.4018
308.15 0.6001 1.4047
308.15 0.7001 1.4072
308.15 0.8002 1.4094
308.15 0.8997 1.4113
308.15 1.0000 1.4129
313.15 0.0000 1.377
313.15 0.1000 1.3831
313.15 0.2000 1.3883
313.15 0.2999 1.3927
313.15 0.3998 1.3964
313.15 0.4999 1.3996
313.15 0.6001 1.4025
313.15 0.7001 1.4049
313.15 0.8002 1.4072
313.15 0.8997 1.4091
313.15 1.0000 1.4108
318.15 0.0000 1.3748
318.15 0.1000 1.3809
318.15 0.2000 1.3861
318.15 0.2999 1.3905
318.15 0.3998 1.3942
318.15 0.4999 1.3974
318.15 0.6001 1.4002
318.15 0.7001 1.4027
318.15 0.8002 1.4049
318.15 0.8997 1.4069
318.15 1.0000 1.4088
323.15 0.0000 1.3726
323.15 0.1000 1.3787
323.15 0.2000 1.3839
323.15 0.2999 1.3882
323.15 0.3998 1.392
323.15 0.4999 1.3952
323.15 0.6001 1.398
323.15 0.7001 1.4005
323.15 0.8002 1.4027
323.15 0.8997 1.4048
323.15 1.0000 1.4067

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 807.75
288.15 0.1000 854.4
288.15 0.2000 891.88
288.15 0.2999 922.67
288.15 0.3998 948.47
288.15 0.4999 970.46
288.15 0.6001 989.43
288.15 0.7001 1005.92
288.15 0.8002 1020.45
288.15 0.8997 1033.27
288.15 1.0000 1044.83
293.15 0.0000 803.77
293.15 0.1000 850.08
293.15 0.2000 887.33
293.15 0.2999 917.95
293.15 0.3998 943.61
293.15 0.4999 965.5
293.15 0.6001 984.4
293.15 0.7001 1000.83
293.15 0.8002 1015.31
293.15 0.8997 1028.1
293.15 1.0000 1039.63
298.15 0.0000 799.76
298.15 0.1000 845.75
298.15 0.2000 882.77
298.15 0.2999 913.21
298.15 0.3998 938.75
298.15 0.4999 960.54
298.15 0.6001 979.36
298.15 0.7001 995.74
298.15 0.8002 1010.18
298.15 0.8997 1022.93
298.15 1.0000 1034.44
303.15 0.0000 795.72
303.15 0.1000 841.4
303.15 0.2000 878.18
303.15 0.2999 908.46
303.15 0.3998 933.87
303.15 0.4999 955.57
303.15 0.6001 974.32
303.15 0.7001 990.64
303.15 0.8002 1005.04
303.15 0.8997 1017.76
303.15 1.0000 1029.25
308.15 0.0000 791.64
308.15 0.1000 837.02
308.15 0.2000 873.57
308.15 0.2999 903.69
308.15 0.3998 928.98
308.15 0.4999 950.59
308.15 0.6001 969.27
308.15 0.7001 985.54
308.15 0.8002 999.9
308.15 0.8997 1012.6
308.15 1.0000 1024.08
313.15 0.0000 787.52
313.15 0.1000 832.6
313.15 0.2000 868.94
313.15 0.2999 898.89
313.15 0.3998 924.07
313.15 0.4999 945.59
313.15 0.6001 964.21
313.15 0.7001 980.44
313.15 0.8002 994.77
313.15 0.8997 1007.44
313.15 1.0000 1018.9
318.15 0.0000 783.36
318.15 0.1000 828.14
318.15 0.2000 864.27
318.15 0.2999 894.07
318.15 0.3998 919.14
318.15 0.4999 940.58
318.15 0.6001 959.14
318.15 0.7001 975.33
318.15 0.8002 989.62
318.15 0.8997 1002.28
318.15 1.0000 1013.72
323.15 0.0000 779.14
323.15 0.1000 823.65
323.15 0.2000 859.57
323.15 0.2999 889.22
323.15 0.3998 914.18
323.15 0.4999 935.55
323.15 0.6001 954.05
323.15 0.7001 970.21
323.15 0.8002 984.48
323.15 0.8997 997.12
323.15 1.0000 1008.55

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 807.75
288.15 0.1000 854.4
288.15 0.2000 891.88
288.15 0.2999 922.67
288.15 0.3998 948.47
288.15 0.4999 970.46
288.15 0.6001 989.43
288.15 0.7001 1005.92
288.15 0.8002 1020.45
288.15 0.8997 1033.27
288.15 1.0000 1044.83
293.15 0.0000 803.77
293.15 0.1000 850.08
293.15 0.2000 887.33
293.15 0.2999 917.95
293.15 0.3998 943.61
293.15 0.4999 965.5
293.15 0.6001 984.4
293.15 0.7001 1000.83
293.15 0.8002 1015.31
293.15 0.8997 1028.1
293.15 1.0000 1039.63
298.15 0.0000 799.76
298.15 0.1000 845.75
298.15 0.2000 882.77
298.15 0.2999 913.21
298.15 0.3998 938.75
298.15 0.4999 960.54
298.15 0.6001 979.36
298.15 0.7001 995.74
298.15 0.8002 1010.18
298.15 0.8997 1022.93
298.15 1.0000 1034.44
303.15 0.0000 795.72
303.15 0.1000 841.4
303.15 0.2000 878.18
303.15 0.2999 908.46
303.15 0.3998 933.87
303.15 0.4999 955.57
303.15 0.6001 974.32
303.15 0.7001 990.64
303.15 0.8002 1005.04
303.15 0.8997 1017.76
303.15 1.0000 1029.25
308.15 0.0000 791.64
308.15 0.1000 837.02
308.15 0.2000 873.57
308.15 0.2999 903.69
308.15 0.3998 928.98
308.15 0.4999 950.59
308.15 0.6001 969.27
308.15 0.7001 985.54
308.15 0.8002 999.9
308.15 0.8997 1012.6
308.15 1.0000 1024.08
313.15 0.0000 787.52
313.15 0.1000 832.6
313.15 0.2000 868.94
313.15 0.2999 898.89
313.15 0.3998 924.07
313.15 0.4999 945.59
313.15 0.6001 964.21
313.15 0.7001 980.44
313.15 0.8002 994.77
313.15 0.8997 1007.44
313.15 1.0000 1018.9
318.15 0.0000 783.36
318.15 0.1000 828.14
318.15 0.2000 864.27
318.15 0.2999 894.07
318.15 0.3998 919.14
318.15 0.4999 940.58
318.15 0.6001 959.14
318.15 0.7001 975.33
318.15 0.8002 989.62
318.15 0.8997 1002.28
318.15 1.0000 1013.72
323.15 0.0000 779.14
323.15 0.1000 823.65
323.15 0.2000 859.57
323.15 0.2999 889.22
323.15 0.3998 914.18
323.15 0.4999 935.55
323.15 0.6001 954.05
323.15 0.7001 970.21
323.15 0.8002 984.48
323.15 0.8997 997.12
323.15 1.0000 1008.55

Sources