Mixture of Carbon dioxide + N,N-Dimethylaminoethanol + Water

Datasets

1. Mass fraction (2)
2. η - Viscosity, Pa*s (4)
3. ρ_l - Mass density, kg/m3 (6)

Mass fraction of Carbon dioxide (1) [ref]

Operational condition: Solvent: Molality, mol/kg = 2.48 (Liquid)

Fixed		Measured
Pressure, kPa of Carbon dioxide (1) - Gas	Temperature, K - Liquid	Mass fraction of Carbon dioxide (1) - Liquid
8.10	298.15	0.0582
8.10	303.15	0.0560
8.10	308.15	0.0525
8.10	313.15	0.0479
15.00	298.15	0.0643
15.00	303.15	0.0629
15.00	308.15	0.0604
15.00	313.15	0.0558
20.30	298.15	0.0654
20.30	303.15	0.0642
20.30	308.15	0.0607
20.30	313.15	0.0577
30.40	298.15	0.0675
30.40	303.15	0.0659
30.40	308.15	0.0629
30.40	313.15	0.0608
60.80	298.15	0.0708
60.80	303.15	0.0692
60.80	308.15	0.0680
60.80	313.15	0.0673

Mass fraction of Carbon dioxide (1) [ref]

Operational condition: Solvent: Molality, mol/kg = 2.48 (Liquid)

Fixed		Measured
Pressure, kPa of Carbon dioxide (1) - Gas	Temperature, K - Liquid	Mass fraction of Carbon dioxide (1) - Liquid
8.10	298.15	0.0582
8.10	303.15	0.0560
8.10	308.15	0.0525
8.10	313.15	0.0479
15.00	298.15	0.0643
15.00	303.15	0.0629
15.00	308.15	0.0604
15.00	313.15	0.0558
20.30	298.15	0.0654
20.30	303.15	0.0642
20.30	308.15	0.0607
20.30	313.15	0.0577
30.40	298.15	0.0675
30.40	303.15	0.0659
30.40	308.15	0.0629
30.40	313.15	0.0608
60.80	298.15	0.0708
60.80	303.15	0.0692
60.80	308.15	0.0680
60.80	313.15	0.0673

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of N,N-Dimethylaminoethanol (2) - Liquid	Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (1) - Liquid	Viscosity, Pa*s - Liquid
0.1500	303.15	0.0000	0.0014
0.1500	303.15	0.7900	0.0015
0.1500	303.15	1.4	0.0015
0.1500	313.15	0.0000	0.0011
0.1500	313.15	0.7900	0.0012
0.1500	313.15	1.4	0.0012
0.1500	323.15	0.0000	0.0009
0.1500	323.15	0.7900	0.0009
0.1500	333.15	0.0000	0.0007
0.1500	333.15	0.7900	0.0008
0.1500	343.15	0.0000	0.0006
0.1500	353.15	0.0000	0.0005
0.3000	303.15	0.0000	0.0029
0.3000	303.15	0.8800	0.0030
0.3000	303.15	1.45	0.0032
0.3000	313.15	0.0000	0.0021
0.3000	313.15	0.8800	0.0022
0.3000	313.15	1.45	0.0024
0.3000	323.15	0.0000	0.0016
0.3000	323.15	0.8800	0.0017
0.3000	323.15	1.45	0.0019
0.3000	333.15	0.0000	0.0012
0.3000	333.15	0.8800	0.0013
0.3000	333.15	1.45	0.0014
0.3000	343.15	0.0000	0.0010
0.3000	343.15	0.8800	0.0011
0.3000	353.15	0.0000	0.0008
0.4500	303.15	0.0000	0.0052
0.4500	303.15	0.4000	0.0058
0.4500	303.15	0.7600	0.0061
0.4500	303.15	1.16	0.0066
0.4500	303.15	1.72	0.0073
0.4500	303.15	2.02	0.0077
0.4500	303.15	2.42	0.0084
0.4500	313.15	0.0000	0.0035
0.4500	313.15	0.4000	0.0040
0.4500	313.15	0.7600	0.0042
0.4500	313.15	1.16	0.0046
0.4500	313.15	1.72	0.0050
0.4500	313.15	2.02	0.0053
0.4500	313.15	2.42	0.0059
0.4500	323.15	0.0000	0.0025
0.4500	323.15	0.4000	0.0028
0.4500	323.15	0.7600	0.0030
0.4500	323.15	1.16	0.0033
0.4500	323.15	1.72	0.0036
0.4500	323.15	2.02	0.0039
0.4500	323.15	2.42	0.0043
0.4500	333.15	0.0000	0.0019
0.4500	333.15	0.4000	0.0021
0.4500	333.15	0.7600	0.0022
0.4500	333.15	1.16	0.0024
0.4500	333.15	1.72	0.0027
0.4500	333.15	2.02	0.0029
0.4500	333.15	2.42	0.0032
0.4500	343.15	0.0000	0.0014
0.4500	343.15	0.4000	0.0016
0.4500	343.15	0.7600	0.0017
0.4500	343.15	1.16	0.0019
0.4500	353.15	0.0000	0.0012
0.4500	353.15	0.4000	0.0013
0.4500	353.15	0.7600	0.0014
0.4500	353.15	1.16	0.0015

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of N,N-Dimethylaminoethanol (2) - Liquid	Molality, mol/kg of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.3000	0.6100	303.15	0.0030
0.3000	0.6100	313.15	0.0022
0.3000	0.6100	323.15	0.0016
0.3000	0.6100	333.15	0.0013
0.3000	0.6100	343.15	0.0010
0.3000	0.6100	353.15	0.0008
0.3000	1.14	303.15	0.0031
0.3000	1.14	313.15	0.0023
0.3000	1.14	323.15	0.0017
0.3000	1.14	333.15	0.0014
0.3000	1.14	343.15	0.0011
0.3000	1.14	353.15	0.0009
0.3000	1.65	303.15	0.0032
0.3000	1.65	313.15	0.0024
0.3000	1.65	323.15	0.0018
0.3000	1.65	333.15	0.0015
0.3000	1.65	343.15	0.0012
0.4000	0.7200	293.15	0.0076
0.4000	0.7200	303.15	0.0050
0.4000	0.7200	313.15	0.0034
0.4000	0.7200	323.15	0.0025
0.4000	0.7200	333.15	0.0019
0.4000	0.7200	343.15	0.0015
0.4000	0.7200	353.15	0.0012
0.4000	1.39	303.15	0.0057
0.4000	1.39	313.15	0.0040
0.4000	1.39	323.15	0.0029
0.4000	1.39	333.15	0.0022
0.4000	2.02	293.15	0.0089
0.4000	2.02	303.15	0.0060
0.4000	2.02	313.15	0.0043
0.4000	2.02	323.15	0.0032
0.4000	2.02	333.15	0.0024

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of N,N-Dimethylaminoethanol (2) - Liquid	Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (1) - Liquid	Viscosity, Pa*s - Liquid
0.1500	303.15	0.0000	0.0014
0.1500	303.15	0.7900	0.0015
0.1500	303.15	1.4	0.0015
0.1500	313.15	0.0000	0.0011
0.1500	313.15	0.7900	0.0012
0.1500	313.15	1.4	0.0012
0.1500	323.15	0.0000	0.0009
0.1500	323.15	0.7900	0.0009
0.1500	333.15	0.0000	0.0007
0.1500	333.15	0.7900	0.0008
0.1500	343.15	0.0000	0.0006
0.1500	353.15	0.0000	0.0005
0.3000	303.15	0.0000	0.0029
0.3000	303.15	0.8800	0.0030
0.3000	303.15	1.45	0.0032
0.3000	313.15	0.0000	0.0021
0.3000	313.15	0.8800	0.0022
0.3000	313.15	1.45	0.0024
0.3000	323.15	0.0000	0.0016
0.3000	323.15	0.8800	0.0017
0.3000	323.15	1.45	0.0019
0.3000	333.15	0.0000	0.0012
0.3000	333.15	0.8800	0.0013
0.3000	333.15	1.45	0.0014
0.3000	343.15	0.0000	0.0010
0.3000	343.15	0.8800	0.0011
0.3000	353.15	0.0000	0.0008
0.4500	303.15	0.0000	0.0052
0.4500	303.15	0.4000	0.0058
0.4500	303.15	0.7600	0.0061
0.4500	303.15	1.16	0.0066
0.4500	303.15	1.72	0.0073
0.4500	303.15	2.02	0.0077
0.4500	303.15	2.42	0.0084
0.4500	313.15	0.0000	0.0035
0.4500	313.15	0.4000	0.0040
0.4500	313.15	0.7600	0.0042
0.4500	313.15	1.16	0.0046
0.4500	313.15	1.72	0.0050
0.4500	313.15	2.02	0.0053
0.4500	313.15	2.42	0.0059
0.4500	323.15	0.0000	0.0025
0.4500	323.15	0.4000	0.0028
0.4500	323.15	0.7600	0.0030
0.4500	323.15	1.16	0.0033
0.4500	323.15	1.72	0.0036
0.4500	323.15	2.02	0.0039
0.4500	323.15	2.42	0.0043
0.4500	333.15	0.0000	0.0019
0.4500	333.15	0.4000	0.0021
0.4500	333.15	0.7600	0.0022
0.4500	333.15	1.16	0.0024
0.4500	333.15	1.72	0.0027
0.4500	333.15	2.02	0.0029
0.4500	333.15	2.42	0.0032
0.4500	343.15	0.0000	0.0014
0.4500	343.15	0.4000	0.0016
0.4500	343.15	0.7600	0.0017
0.4500	343.15	1.16	0.0019
0.4500	353.15	0.0000	0.0012
0.4500	353.15	0.4000	0.0013
0.4500	353.15	0.7600	0.0014
0.4500	353.15	1.16	0.0015

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of N,N-Dimethylaminoethanol (2) - Liquid	Molality, mol/kg of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.3000	0.6100	303.15	0.0030
0.3000	0.6100	313.15	0.0022
0.3000	0.6100	323.15	0.0016
0.3000	0.6100	333.15	0.0013
0.3000	0.6100	343.15	0.0010
0.3000	0.6100	353.15	0.0008
0.3000	1.14	303.15	0.0031
0.3000	1.14	313.15	0.0023
0.3000	1.14	323.15	0.0017
0.3000	1.14	333.15	0.0014
0.3000	1.14	343.15	0.0011
0.3000	1.14	353.15	0.0009
0.3000	1.65	303.15	0.0032
0.3000	1.65	313.15	0.0024
0.3000	1.65	323.15	0.0018
0.3000	1.65	333.15	0.0015
0.3000	1.65	343.15	0.0012
0.4000	0.7200	293.15	0.0076
0.4000	0.7200	303.15	0.0050
0.4000	0.7200	313.15	0.0034
0.4000	0.7200	323.15	0.0025
0.4000	0.7200	333.15	0.0019
0.4000	0.7200	343.15	0.0015
0.4000	0.7200	353.15	0.0012
0.4000	1.39	303.15	0.0057
0.4000	1.39	313.15	0.0040
0.4000	1.39	323.15	0.0029
0.4000	1.39	333.15	0.0022
0.4000	2.02	293.15	0.0089
0.4000	2.02	303.15	0.0060
0.4000	2.02	313.15	0.0043
0.4000	2.02	323.15	0.0032
0.4000	2.02	333.15	0.0024

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of N,N-Dimethylaminoethanol (2) - Liquid	Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (1) - Liquid	Mass density, kg/m3 - Liquid
0.1500	298.15	0.0000	992.33
0.1500	298.15	0.7900	1026.83
0.1500	298.15	1.38	1052.93
0.1500	303.15	0.0000	990.35
0.1500	303.15	0.7900	1026.25
0.1500	303.15	1.38	1050.61
0.1500	313.15	0.0000	985.86
0.1500	313.15	0.7900	1021.07
0.1500	313.15	1.38	1046.01
0.1500	323.15	0.0000	980.82
0.1500	323.15	0.7900	1015.39
0.1500	333.15	0.0000	975.14
0.1500	333.15	0.7900	1009.3
0.1500	343.15	0.0000	968.93
0.1500	343.15	0.7900	1002.83
0.1500	353.15	0.0000	962.24
0.3000	298.15	0.0000	988.0
0.3000	298.15	0.8800	1026.8
0.3000	298.15	1.45	1051.32
0.3000	299.15	0.0000	987.42
0.3000	299.15	0.8800	1026.17
0.3000	299.15	1.45	1050.68
0.3000	301.15	0.0000	986.26
0.3000	301.15	0.8800	1024.9
0.3000	301.15	1.45	1049.4
0.3000	303.15	0.0000	985.08
0.3000	303.15	0.8800	1023.62
0.3000	303.15	1.45	1048.1
0.3000	313.15	0.0000	978.92
0.3000	313.15	0.8800	1016.97
0.3000	313.15	1.45	1041.39
0.3000	323.15	0.0000	972.34
0.3000	323.15	0.8800	1010.0
0.3000	323.15	1.45	1034.4
0.3000	333.15	0.0000	965.36
0.3000	333.15	0.8800	1002.73
0.3000	333.15	1.45	1027.18
0.3000	343.15	0.0000	957.98
0.3000	343.15	0.8800	995.21
0.3000	353.15	0.0000	950.22
0.4500	298.15	0.0000	980.4
0.4500	298.15	0.4500	999.85
0.4500	298.15	0.7600	1013.95
0.4500	298.15	1.16	1030.42
0.4500	298.15	1.67	1054.79
0.4500	298.15	2.22	1077.04
0.4500	298.15	2.42	1086.03
0.4500	303.15	0.0000	976.75
0.4500	303.15	0.4500	996.08
0.4500	303.15	0.7600	1010.13
0.4500	303.15	1.16	1026.6
0.4500	303.15	1.67	1050.96
0.4500	303.15	2.22	1073.27
0.4500	303.15	2.42	1082.32
0.4500	313.15	0.0000	969.32
0.4500	313.15	0.4500	988.4
0.4500	313.15	0.7600	1002.39
0.4500	313.15	1.16	1018.81
0.4500	313.15	1.67	1043.2
0.4500	313.15	2.22	1065.67
0.4500	313.15	2.42	1074.82
0.4500	323.15	0.0000	961.69
0.4500	323.15	0.4500	980.51
0.4500	323.15	0.7600	994.47
0.4500	323.15	1.16	1010.89
0.4500	323.15	1.67	1035.36
0.4500	323.15	2.22	1058.01
0.4500	323.15	2.42	1067.24
0.4500	333.15	0.0000	953.66
0.4500	333.15	0.4500	972.39
0.4500	333.15	0.7600	986.38
0.4500	333.15	1.16	1002.83
0.4500	333.15	1.67	1027.4
0.4500	333.15	2.22	1050.25
0.4500	343.15	0.0000	945.33
0.4500	343.15	0.4500	964.04
0.4500	343.15	0.7600	978.08
0.4500	343.15	1.16	994.59
0.4500	353.15	0.0000	936.72
0.4500	353.15	0.4500	955.38
0.4500	353.15	0.7600	969.55
0.4500	353.15	1.16	986.13

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Solvent: Mass fraction = 0.3 (Liquid)

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0079	293.15	1008.4
0.0079	298.15	1005.5
0.0079	303.15	1002.5
0.0079	308.15	999.5
0.0079	313.15	996.2
0.0079	318.15	992.8
0.0079	323.15	989.2
0.0079	328.15	985.8
0.0079	333.15	982.4
0.0079	338.15	977.9
0.0079	343.15	974.0
0.0157	293.15	1023.7
0.0157	298.15	1020.8
0.0157	303.15	1017.7
0.0157	308.15	1014.5
0.0157	313.15	1011.2
0.0157	318.15	1007.6
0.0157	323.15	1003.9
0.0157	328.15	999.9
0.0157	333.15	995.4
0.0157	338.15	991.1
0.0157	343.15	986.4
0.0211	293.15	1029.3
0.0211	298.15	1026.2
0.0211	303.15	1023.1
0.0211	308.15	1019.9
0.0211	313.15	1016.6
0.0211	318.15	1013.1
0.0211	323.15	1009.6
0.0211	328.15	1006.2
0.0211	333.15	1002.5
0.0211	338.15	998.5
0.0211	343.15	993.7
0.0310	293.15	1051.2
0.0310	298.15	1048.2
0.0310	303.15	1045.0
0.0310	308.15	1041.8
0.0310	313.15	1038.4
0.0310	318.15	1035.0
0.0310	323.15	1031.5
0.0310	328.15	1028.0
0.0310	333.15	1024.3
0.0310	338.15	1020.7
0.0310	343.15	1016.9
0.0414	293.15	1063.7
0.0414	298.15	1060.7
0.0414	303.15	1057.6
0.0414	308.15	1054.4
0.0414	313.15	1051.1
0.0414	318.15	1047.7
0.0414	323.15	1044.3
0.0414	328.15	1040.8
0.0414	333.15	1037.3
0.0414	338.15	1033.7
0.0414	343.15	1030.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Molality, mol/kg of Carbon dioxide (1) - Liquid	Solvent: Mass fraction of N,N-Dimethylaminoethanol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.6100	0.3000	298.15	1013.83
0.6100	0.3000	303.15	1010.74
0.6100	0.3000	313.15	1004.24
0.6100	0.3000	323.15	997.36
0.6100	0.3000	333.15	990.15
0.6100	0.3000	343.15	982.63
0.6100	0.3000	353.15	974.83
1.14	0.3000	298.15	1037.76
1.14	0.3000	303.15	1034.54
1.14	0.3000	313.15	1027.82
1.14	0.3000	323.15	1020.8
1.14	0.3000	333.15	1013.52
1.14	0.3000	343.15	1006.0
1.14	0.3000	353.15	998.27
1.65	0.3000	298.15	1060.16
1.65	0.3000	303.15	1056.93
1.65	0.3000	313.15	1050.28
1.65	0.3000	323.15	1043.36
1.65	0.3000	333.15	1036.22
1.65	0.3000	343.15	1028.82
1.65	0.3000	353.15	1021.17
2.42	0.3000	298.15	1093.53
2.42	0.3000	303.15	1090.8
2.42	0.3000	313.15	1085.16
0.7200	0.4000	298.15	1013.99
0.7200	0.4000	303.15	1010.37
0.7200	0.4000	313.15	1002.95
0.7200	0.4000	323.15	995.31
0.7200	0.4000	333.15	987.46
0.7200	0.4000	343.15	979.4
0.7200	0.4000	353.15	971.08
1.39	0.4000	298.15	1043.19
1.39	0.4000	303.15	1039.49
1.39	0.4000	313.15	1031.97
1.39	0.4000	323.15	1024.27
1.39	0.4000	333.15	1016.45
1.39	0.4000	343.15	1008.46
1.39	0.4000	353.15	1000.26
2.02	0.4000	303.15	1067.05
2.02	0.4000	313.15	1059.66
2.02	0.4000	323.15	1052.14
2.02	0.4000	333.15	1044.51
2.02	0.4000	343.15	1036.74
2.65	0.4000	303.15	1094.95
2.65	0.4000	313.15	1088.07
2.65	0.4000	323.15	1081.07
2.65	0.4000	333.15	1073.88

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of N,N-Dimethylaminoethanol (2) - Liquid	Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (1) - Liquid	Mass density, kg/m3 - Liquid
0.1500	298.15	0.0000	992.33
0.1500	298.15	0.7900	1026.83
0.1500	298.15	1.38	1052.93
0.1500	303.15	0.0000	990.35
0.1500	303.15	0.7900	1026.25
0.1500	303.15	1.38	1050.61
0.1500	313.15	0.0000	985.86
0.1500	313.15	0.7900	1021.07
0.1500	313.15	1.38	1046.01
0.1500	323.15	0.0000	980.82
0.1500	323.15	0.7900	1015.39
0.1500	333.15	0.0000	975.14
0.1500	333.15	0.7900	1009.3
0.1500	343.15	0.0000	968.93
0.1500	343.15	0.7900	1002.83
0.1500	353.15	0.0000	962.24
0.3000	298.15	0.0000	988.0
0.3000	298.15	0.8800	1026.8
0.3000	298.15	1.45	1051.32
0.3000	299.15	0.0000	987.42
0.3000	299.15	0.8800	1026.17
0.3000	299.15	1.45	1050.68
0.3000	301.15	0.0000	986.26
0.3000	301.15	0.8800	1024.9
0.3000	301.15	1.45	1049.4
0.3000	303.15	0.0000	985.08
0.3000	303.15	0.8800	1023.62
0.3000	303.15	1.45	1048.1
0.3000	313.15	0.0000	978.92
0.3000	313.15	0.8800	1016.97
0.3000	313.15	1.45	1041.39
0.3000	323.15	0.0000	972.34
0.3000	323.15	0.8800	1010.0
0.3000	323.15	1.45	1034.4
0.3000	333.15	0.0000	965.36
0.3000	333.15	0.8800	1002.73
0.3000	333.15	1.45	1027.18
0.3000	343.15	0.0000	957.98
0.3000	343.15	0.8800	995.21
0.3000	353.15	0.0000	950.22
0.4500	298.15	0.0000	980.4
0.4500	298.15	0.4500	999.85
0.4500	298.15	0.7600	1013.95
0.4500	298.15	1.16	1030.42
0.4500	298.15	1.67	1054.79
0.4500	298.15	2.22	1077.04
0.4500	298.15	2.42	1086.03
0.4500	303.15	0.0000	976.75
0.4500	303.15	0.4500	996.08
0.4500	303.15	0.7600	1010.13
0.4500	303.15	1.16	1026.6
0.4500	303.15	1.67	1050.96
0.4500	303.15	2.22	1073.27
0.4500	303.15	2.42	1082.32
0.4500	313.15	0.0000	969.32
0.4500	313.15	0.4500	988.4
0.4500	313.15	0.7600	1002.39
0.4500	313.15	1.16	1018.81
0.4500	313.15	1.67	1043.2
0.4500	313.15	2.22	1065.67
0.4500	313.15	2.42	1074.82
0.4500	323.15	0.0000	961.69
0.4500	323.15	0.4500	980.51
0.4500	323.15	0.7600	994.47
0.4500	323.15	1.16	1010.89
0.4500	323.15	1.67	1035.36
0.4500	323.15	2.22	1058.01
0.4500	323.15	2.42	1067.24
0.4500	333.15	0.0000	953.66
0.4500	333.15	0.4500	972.39
0.4500	333.15	0.7600	986.38
0.4500	333.15	1.16	1002.83
0.4500	333.15	1.67	1027.4
0.4500	333.15	2.22	1050.25
0.4500	343.15	0.0000	945.33
0.4500	343.15	0.4500	964.04
0.4500	343.15	0.7600	978.08
0.4500	343.15	1.16	994.59
0.4500	353.15	0.0000	936.72
0.4500	353.15	0.4500	955.38
0.4500	353.15	0.7600	969.55
0.4500	353.15	1.16	986.13

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Solvent: Mass fraction = 0.3 (Liquid)

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0079	293.15	1008.4
0.0079	298.15	1005.5
0.0079	303.15	1002.5
0.0079	308.15	999.5
0.0079	313.15	996.2
0.0079	318.15	992.8
0.0079	323.15	989.2
0.0079	328.15	985.8
0.0079	333.15	982.4
0.0079	338.15	977.9
0.0079	343.15	974.0
0.0157	293.15	1023.7
0.0157	298.15	1020.8
0.0157	303.15	1017.7
0.0157	308.15	1014.5
0.0157	313.15	1011.2
0.0157	318.15	1007.6
0.0157	323.15	1003.9
0.0157	328.15	999.9
0.0157	333.15	995.4
0.0157	338.15	991.1
0.0157	343.15	986.4
0.0211	293.15	1029.3
0.0211	298.15	1026.2
0.0211	303.15	1023.1
0.0211	308.15	1019.9
0.0211	313.15	1016.6
0.0211	318.15	1013.1
0.0211	323.15	1009.6
0.0211	328.15	1006.2
0.0211	333.15	1002.5
0.0211	338.15	998.5
0.0211	343.15	993.7
0.0310	293.15	1051.2
0.0310	298.15	1048.2
0.0310	303.15	1045.0
0.0310	308.15	1041.8
0.0310	313.15	1038.4
0.0310	318.15	1035.0
0.0310	323.15	1031.5
0.0310	328.15	1028.0
0.0310	333.15	1024.3
0.0310	338.15	1020.7
0.0310	343.15	1016.9
0.0414	293.15	1063.7
0.0414	298.15	1060.7
0.0414	303.15	1057.6
0.0414	308.15	1054.4
0.0414	313.15	1051.1
0.0414	318.15	1047.7
0.0414	323.15	1044.3
0.0414	328.15	1040.8
0.0414	333.15	1037.3
0.0414	338.15	1033.7
0.0414	343.15	1030.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Molality, mol/kg of Carbon dioxide (1) - Liquid	Solvent: Mass fraction of N,N-Dimethylaminoethanol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.6100	0.3000	298.15	1013.83
0.6100	0.3000	303.15	1010.74
0.6100	0.3000	313.15	1004.24
0.6100	0.3000	323.15	997.36
0.6100	0.3000	333.15	990.15
0.6100	0.3000	343.15	982.63
0.6100	0.3000	353.15	974.83
1.14	0.3000	298.15	1037.76
1.14	0.3000	303.15	1034.54
1.14	0.3000	313.15	1027.82
1.14	0.3000	323.15	1020.8
1.14	0.3000	333.15	1013.52
1.14	0.3000	343.15	1006.0
1.14	0.3000	353.15	998.27
1.65	0.3000	298.15	1060.16
1.65	0.3000	303.15	1056.93
1.65	0.3000	313.15	1050.28
1.65	0.3000	323.15	1043.36
1.65	0.3000	333.15	1036.22
1.65	0.3000	343.15	1028.82
1.65	0.3000	353.15	1021.17
2.42	0.3000	298.15	1093.53
2.42	0.3000	303.15	1090.8
2.42	0.3000	313.15	1085.16
0.7200	0.4000	298.15	1013.99
0.7200	0.4000	303.15	1010.37
0.7200	0.4000	313.15	1002.95
0.7200	0.4000	323.15	995.31
0.7200	0.4000	333.15	987.46
0.7200	0.4000	343.15	979.4
0.7200	0.4000	353.15	971.08
1.39	0.4000	298.15	1043.19
1.39	0.4000	303.15	1039.49
1.39	0.4000	313.15	1031.97
1.39	0.4000	323.15	1024.27
1.39	0.4000	333.15	1016.45
1.39	0.4000	343.15	1008.46
1.39	0.4000	353.15	1000.26
2.02	0.4000	303.15	1067.05
2.02	0.4000	313.15	1059.66
2.02	0.4000	323.15	1052.14
2.02	0.4000	333.15	1044.51
2.02	0.4000	343.15	1036.74
2.65	0.4000	303.15	1094.95
2.65	0.4000	313.15	1088.07
2.65	0.4000	323.15	1081.07
2.65	0.4000	333.15	1073.88

Sources

• CO2 absorption with aqueous tertiary amine solutions: Equilibrium solubility and thermodynamic modeling
• Density and Viscosity of Partially Carbonated Aqueous Tertiary Alkanolamine Solutions at Temperatures between (298.15 and 353.15) K
• Densities of Aqueous 2-Dimethylaminoethanol Solutions at Temperatures of (293.15 to 343.15) K
• Density and Viscosity of Partially Carbonated Aqueous Solutions Containing a Tertiary Alkanolamine and Piperazine at Temperatures between 298.15 and 353.15 K