Mixture of Diethanolamine + Ethanol, 2-(2-butoxyethoxy)-

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.8909
293.15	0.0330	0.6813
293.15	0.0672	0.5502
293.15	0.1026	0.4251
293.15	0.1394	0.3213
293.15	0.2174	0.1916
293.15	0.3018	0.1144
293.15	0.3933	0.0652
293.15	0.4929	0.0386
293.15	0.6019	0.0238
293.15	0.7008	0.0158
293.15	0.7558	0.0122
293.15	0.8059	0.0104
293.15	0.8537	0.0090
293.15	0.9031	0.0079
293.15	1.0000	0.0058
303.15	0.0000	0.3822
303.15	0.0330	0.2907
303.15	0.0672	0.2316
303.15	0.1026	0.1899
303.15	0.1394	0.1501
303.15	0.2174	0.0962
303.15	0.3018	0.0600
303.15	0.3933	0.0370
303.15	0.4929	0.0228
303.15	0.6019	0.0149
303.15	0.7008	0.0104
303.15	0.7558	0.0088
303.15	0.8059	0.0073
303.15	0.8537	0.0063
303.15	0.9031	0.0055
303.15	1.0000	0.0042
313.15	0.0000	0.1876
313.15	0.0330	0.1562
313.15	0.0672	0.1225
313.15	0.1026	0.0982
313.15	0.1394	0.0811
313.15	0.2174	0.0533
313.15	0.3018	0.0345
313.15	0.3933	0.0223
313.15	0.4929	0.0148
313.15	0.6019	0.0100
313.15	0.7008	0.0073
313.15	0.7558	0.0060
313.15	0.8059	0.0053
313.15	0.8537	0.0046
313.15	0.9031	0.0040
313.15	1.0000	0.0032
323.15	0.0000	0.0991
323.15	0.0330	0.0800
323.15	0.0672	0.0663
323.15	0.1026	0.0539
323.15	0.1394	0.0432
323.15	0.2174	0.0304
323.15	0.3018	0.0207
323.15	0.3933	0.0143
323.15	0.4929	0.0094
323.15	0.6019	0.0070
323.15	0.7008	0.0052
323.15	0.7558	0.0043
323.15	0.8059	0.0038
323.15	0.8537	0.0034
323.15	0.9031	0.0030
323.15	1.0000	0.0025
333.15	0.0000	0.0581
333.15	0.0330	0.0467
333.15	0.0672	0.0385
333.15	0.1026	0.0320
333.15	0.1394	0.0267
333.15	0.2174	0.0191
333.15	0.3018	0.0132
333.15	0.3933	0.0094
333.15	0.4929	0.0070
333.15	0.6019	0.0052
333.15	0.7008	0.0039
333.15	0.7558	0.0034
333.15	0.8059	0.0030
333.15	0.8537	0.0028
333.15	0.9031	0.0025
333.15	1.0000	0.0020

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.8909
293.15	0.0330	0.6813
293.15	0.0672	0.5502
293.15	0.1026	0.4251
293.15	0.1394	0.3213
293.15	0.2174	0.1916
293.15	0.3018	0.1144
293.15	0.3933	0.0652
293.15	0.4929	0.0386
293.15	0.6019	0.0238
293.15	0.7008	0.0158
293.15	0.7558	0.0122
293.15	0.8059	0.0104
293.15	0.8537	0.0090
293.15	0.9031	0.0079
293.15	1.0000	0.0058
303.15	0.0000	0.3822
303.15	0.0330	0.2907
303.15	0.0672	0.2316
303.15	0.1026	0.1899
303.15	0.1394	0.1501
303.15	0.2174	0.0962
303.15	0.3018	0.0600
303.15	0.3933	0.0370
303.15	0.4929	0.0228
303.15	0.6019	0.0149
303.15	0.7008	0.0104
303.15	0.7558	0.0088
303.15	0.8059	0.0073
303.15	0.8537	0.0063
303.15	0.9031	0.0055
303.15	1.0000	0.0042
313.15	0.0000	0.1876
313.15	0.0330	0.1562
313.15	0.0672	0.1225
313.15	0.1026	0.0982
313.15	0.1394	0.0811
313.15	0.2174	0.0533
313.15	0.3018	0.0345
313.15	0.3933	0.0223
313.15	0.4929	0.0148
313.15	0.6019	0.0100
313.15	0.7008	0.0073
313.15	0.7558	0.0060
313.15	0.8059	0.0053
313.15	0.8537	0.0046
313.15	0.9031	0.0040
313.15	1.0000	0.0032
323.15	0.0000	0.0991
323.15	0.0330	0.0800
323.15	0.0672	0.0663
323.15	0.1026	0.0539
323.15	0.1394	0.0432
323.15	0.2174	0.0304
323.15	0.3018	0.0207
323.15	0.3933	0.0143
323.15	0.4929	0.0094
323.15	0.6019	0.0070
323.15	0.7008	0.0052
323.15	0.7558	0.0043
323.15	0.8059	0.0038
323.15	0.8537	0.0034
323.15	0.9031	0.0030
323.15	1.0000	0.0025
333.15	0.0000	0.0581
333.15	0.0330	0.0467
333.15	0.0672	0.0385
333.15	0.1026	0.0320
333.15	0.1394	0.0267
333.15	0.2174	0.0191
333.15	0.3018	0.0132
333.15	0.3933	0.0094
333.15	0.4929	0.0070
333.15	0.6019	0.0052
333.15	0.7008	0.0039
333.15	0.7558	0.0034
333.15	0.8059	0.0030
333.15	0.8537	0.0028
333.15	0.9031	0.0025
333.15	1.0000	0.0020

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1096.1
293.15	0.0330	1088.3
293.15	0.0672	1080.7
293.15	0.1026	1073.2
293.15	0.1394	1065.8
293.15	0.2174	1050.9
293.15	0.3018	1036.3
293.15	0.3933	1021.9
293.15	0.4929	1007.7
293.15	0.6019	993.8
293.15	0.7008	982.3
293.15	0.7558	976.4
293.15	0.8059	971.2
293.15	0.8537	966.4
293.15	0.9031	961.6
293.15	1.0000	952.9
303.15	0.0000	1089.8
303.15	0.0330	1081.8
303.15	0.0672	1074.2
303.15	0.1026	1066.5
303.15	0.1394	1058.9
303.15	0.2174	1043.7
303.15	0.3018	1028.7
303.15	0.3933	1014.0
303.15	0.4929	999.5
303.15	0.6019	985.2
303.15	0.7008	973.5
303.15	0.7558	967.5
303.15	0.8059	962.2
303.15	0.8537	957.3
303.15	0.9031	952.4
303.15	1.0000	943.5
313.15	0.0000	1083.7
313.15	0.0330	1075.8
313.15	0.0672	1068.0
313.15	0.1026	1060.3
313.15	0.1394	1052.5
313.15	0.2174	1037.1
313.15	0.3018	1021.9
313.15	0.3933	1007.0
313.15	0.4929	992.3
313.15	0.6019	977.9
313.15	0.7008	966.1
313.15	0.7558	960.0
313.15	0.8059	954.7
313.15	0.8537	949.7
313.15	0.9031	944.8
313.15	1.0000	935.7
323.15	0.0000	1077.4
323.15	0.0330	1069.4
323.15	0.0672	1061.5
323.15	0.1026	1053.6
323.15	0.1394	1045.7
323.15	0.2174	1029.9
323.15	0.3018	1014.5
323.15	0.3933	999.2
323.15	0.4929	984.2
323.15	0.6019	969.6
323.15	0.7008	957.6
323.15	0.7558	951.4
323.15	0.8059	946.0
323.15	0.8537	940.9
323.15	0.9031	935.9
323.15	1.0000	926.6
333.15	0.0000	1070.7
333.15	0.0330	1062.8
333.15	0.0672	1054.9
333.15	0.1026	1046.9
333.15	0.1394	1038.8
333.15	0.2174	1022.8
333.15	0.3018	1007.3
333.15	0.3933	991.8
333.15	0.4929	976.7
333.15	0.6019	961.9
333.15	0.7008	949.8
333.15	0.7558	943.5
333.15	0.8059	938.1
333.15	0.8537	933.0
333.15	0.9031	927.9
333.15	1.0000	918.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1096.1
293.15	0.0330	1088.3
293.15	0.0672	1080.7
293.15	0.1026	1073.2
293.15	0.1394	1065.8
293.15	0.2174	1050.9
293.15	0.3018	1036.3
293.15	0.3933	1021.9
293.15	0.4929	1007.7
293.15	0.6019	993.8
293.15	0.7008	982.3
293.15	0.7558	976.4
293.15	0.8059	971.2
293.15	0.8537	966.4
293.15	0.9031	961.6
293.15	1.0000	952.9
303.15	0.0000	1089.8
303.15	0.0330	1081.8
303.15	0.0672	1074.2
303.15	0.1026	1066.5
303.15	0.1394	1058.9
303.15	0.2174	1043.7
303.15	0.3018	1028.7
303.15	0.3933	1014.0
303.15	0.4929	999.5
303.15	0.6019	985.2
303.15	0.7008	973.5
303.15	0.7558	967.5
303.15	0.8059	962.2
303.15	0.8537	957.3
303.15	0.9031	952.4
303.15	1.0000	943.5
313.15	0.0000	1083.7
313.15	0.0330	1075.8
313.15	0.0672	1068.0
313.15	0.1026	1060.3
313.15	0.1394	1052.5
313.15	0.2174	1037.1
313.15	0.3018	1021.9
313.15	0.3933	1007.0
313.15	0.4929	992.3
313.15	0.6019	977.9
313.15	0.7008	966.1
313.15	0.7558	960.0
313.15	0.8059	954.7
313.15	0.8537	949.7
313.15	0.9031	944.8
313.15	1.0000	935.7
323.15	0.0000	1077.4
323.15	0.0330	1069.4
323.15	0.0672	1061.5
323.15	0.1026	1053.6
323.15	0.1394	1045.7
323.15	0.2174	1029.9
323.15	0.3018	1014.5
323.15	0.3933	999.2
323.15	0.4929	984.2
323.15	0.6019	969.6
323.15	0.7008	957.6
323.15	0.7558	951.4
323.15	0.8059	946.0
323.15	0.8537	940.9
323.15	0.9031	935.9
323.15	1.0000	926.6
333.15	0.0000	1070.7
333.15	0.0330	1062.8
333.15	0.0672	1054.9
333.15	0.1026	1046.9
333.15	0.1394	1038.8
333.15	0.2174	1022.8
333.15	0.3018	1007.3
333.15	0.3933	991.8
333.15	0.4929	976.7
333.15	0.6019	961.9
333.15	0.7008	949.8
333.15	0.7558	943.5
333.15	0.8059	938.1
333.15	0.8537	933.0
333.15	0.9031	927.9
333.15	1.0000	918.5

Sources

• Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K