Mixture of Ethanol, 2-[2-(2-ethoxyethoxy)ethoxy]- + Water

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-(2-ethoxyethoxy)ethoxy]- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0010
293.15	0.0112	0.0015
293.15	0.0249	0.0022
293.15	0.0413	0.0033
293.15	0.0628	0.0048
293.15	0.0918	0.0070
293.15	0.1317	0.0091
293.15	0.1905	0.0105
293.15	0.2885	0.0113
293.15	0.4019	0.0113
293.15	0.4747	0.0109
293.15	0.6076	0.0101
293.15	0.7399	0.0092
293.15	0.8176	0.0087
293.15	0.8956	0.0084
293.15	1.0000	0.0078
298.15	1.0000	0.0067
303.15	0.0000	0.0008
303.15	0.0112	0.0011
303.15	0.0249	0.0016
303.15	0.0413	0.0023
303.15	0.0628	0.0033
303.15	0.0918	0.0046
303.15	0.1317	0.0060
303.15	0.1905	0.0070
303.15	0.2885	0.0075
303.15	0.4019	0.0075
303.15	0.4747	0.0074
303.15	0.6076	0.0069
303.15	0.7399	0.0064
303.15	0.8176	0.0062
303.15	0.8956	0.0059
303.15	1.0000	0.0057
313.15	0.0000	0.0007
313.15	0.0112	0.0009
313.15	0.0249	0.0013
313.15	0.0413	0.0017
313.15	0.0628	0.0024
313.15	0.0918	0.0033
313.15	0.1317	0.0041
313.15	0.1905	0.0049
313.15	0.2885	0.0054
313.15	0.4019	0.0054
313.15	0.4747	0.0052
313.15	0.6076	0.0050
313.15	0.7399	0.0046
313.15	0.8176	0.0045
313.15	0.8956	0.0043
313.15	1.0000	0.0042
323.15	0.0000	0.0005
323.15	0.0112	0.0007
323.15	0.0249	0.0010
323.15	0.0413	0.0014
323.15	0.0628	0.0019
323.15	0.0918	0.0024
323.15	0.1317	0.0030
323.15	0.1905	0.0036
323.15	0.2885	0.0039
323.15	0.4019	0.0040
323.15	0.4747	0.0039
323.15	0.6076	0.0037
323.15	0.7399	0.0036
323.15	0.8176	0.0035
323.15	0.8956	0.0034
323.15	1.0000	0.0033
333.15	0.0000	0.0005
333.15	0.0112	0.0006
333.15	0.0249	0.0008
333.15	0.0413	0.0011
333.15	0.0628	0.0014
333.15	0.0918	0.0019
333.15	0.1317	0.0023
333.15	0.1905	0.0027
333.15	0.2885	0.0029
333.15	0.4019	0.0030
333.15	0.4747	0.0030
333.15	0.6076	0.0029
333.15	0.7399	0.0028
333.15	0.8176	0.0027
333.15	0.8956	0.0027
333.15	1.0000	0.0026

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-[2-(2-ethoxyethoxy)ethoxy]- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0010
293.15	0.0112	0.0015
293.15	0.0249	0.0022
293.15	0.0413	0.0033
293.15	0.0628	0.0048
293.15	0.0918	0.0070
293.15	0.1317	0.0091
293.15	0.1905	0.0105
293.15	0.2885	0.0113
293.15	0.4019	0.0113
293.15	0.4747	0.0109
293.15	0.6076	0.0101
293.15	0.7399	0.0092
293.15	0.8176	0.0087
293.15	0.8956	0.0084
293.15	1.0000	0.0078
298.15	1.0000	0.0067
303.15	0.0000	0.0008
303.15	0.0112	0.0011
303.15	0.0249	0.0016
303.15	0.0413	0.0023
303.15	0.0628	0.0033
303.15	0.0918	0.0046
303.15	0.1317	0.0060
303.15	0.1905	0.0070
303.15	0.2885	0.0075
303.15	0.4019	0.0075
303.15	0.4747	0.0074
303.15	0.6076	0.0069
303.15	0.7399	0.0064
303.15	0.8176	0.0062
303.15	0.8956	0.0059
303.15	1.0000	0.0057
313.15	0.0000	0.0007
313.15	0.0112	0.0009
313.15	0.0249	0.0013
313.15	0.0413	0.0017
313.15	0.0628	0.0024
313.15	0.0918	0.0033
313.15	0.1317	0.0041
313.15	0.1905	0.0049
313.15	0.2885	0.0054
313.15	0.4019	0.0054
313.15	0.4747	0.0052
313.15	0.6076	0.0050
313.15	0.7399	0.0046
313.15	0.8176	0.0045
313.15	0.8956	0.0043
313.15	1.0000	0.0042
323.15	0.0000	0.0005
323.15	0.0112	0.0007
323.15	0.0249	0.0010
323.15	0.0413	0.0014
323.15	0.0628	0.0019
323.15	0.0918	0.0024
323.15	0.1317	0.0030
323.15	0.1905	0.0036
323.15	0.2885	0.0039
323.15	0.4019	0.0040
323.15	0.4747	0.0039
323.15	0.6076	0.0037
323.15	0.7399	0.0036
323.15	0.8176	0.0035
323.15	0.8956	0.0034
323.15	1.0000	0.0033
333.15	0.0000	0.0005
333.15	0.0112	0.0006
333.15	0.0249	0.0008
333.15	0.0413	0.0011
333.15	0.0628	0.0014
333.15	0.0918	0.0019
333.15	0.1317	0.0023
333.15	0.1905	0.0027
333.15	0.2885	0.0029
333.15	0.4019	0.0030
333.15	0.4747	0.0030
333.15	0.6076	0.0029
333.15	0.7399	0.0028
333.15	0.8176	0.0027
333.15	0.8956	0.0027
333.15	1.0000	0.0026

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-[2-(2-ethoxyethoxy)ethoxy]- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	998.2
293.15	0.0112	1006.9
293.15	0.0249	1016.6
293.15	0.0413	1026.2
293.15	0.0628	1035.1
293.15	0.0918	1040.8
293.15	0.1317	1042.7
293.15	0.1905	1042.2
293.15	0.2885	1038.7
293.15	0.4019	1033.6
293.15	0.4747	1031.1
293.15	0.6076	1027.3
293.15	0.7399	1024.4
293.15	0.8176	1022.9
293.15	0.8956	1021.8
293.15	1.0000	1020.6
298.15	1.0000	1016.3
303.15	0.0000	995.7
303.15	0.0112	1003.7
303.15	0.0249	1012.6
303.15	0.0413	1020.7
303.15	0.0628	1028.7
303.15	0.0918	1032.8
303.15	0.1317	1034.9
303.15	0.1905	1033.9
303.15	0.2885	1029.8
303.15	0.4019	1024.9
303.15	0.4747	1022.3
303.15	0.6076	1018.5
303.15	0.7399	1015.5
303.15	0.8176	1014.1
303.15	0.8956	1013.1
303.15	1.0000	1011.9
308.15	1.0000	1008.1
313.15	0.0000	992.2
313.15	0.0112	999.7
313.15	0.0249	1007.5
313.15	0.0413	1014.8
313.15	0.0628	1021.8
313.15	0.0918	1025.3
313.15	0.1317	1026.5
313.15	0.1905	1025.5
313.15	0.2885	1021.4
313.15	0.4019	1016.5
313.15	0.4747	1013.9
313.15	0.6076	1010.2
313.15	0.7399	1007.4
313.15	0.8176	1006.1
313.15	0.8956	1005.1
313.15	1.0000	1003.9
323.15	0.0000	988.1
323.15	0.0112	995.1
323.15	0.0249	1002.1
323.15	0.0413	1008.7
323.15	0.0628	1014.4
323.15	0.0918	1017.4
323.15	0.1317	1018.1
323.15	0.1905	1016.8
323.15	0.2885	1012.7
323.15	0.4019	1007.7
323.15	0.4747	1005.2
323.15	0.6076	1001.6
323.15	0.7399	998.8
323.15	0.8176	997.6
323.15	0.8956	996.6
323.15	1.0000	995.5
333.15	0.0000	983.2
333.15	0.0112	989.6
333.15	0.0249	995.7
333.15	0.0413	1001.9
333.15	0.0628	1006.2
333.15	0.0918	1008.5
333.15	0.1317	1008.7
333.15	0.1905	1007.3
333.15	0.2885	1003.1
333.15	0.4019	998.5
333.15	0.4747	996.1
333.15	0.6076	992.5
333.15	0.7399	989.8
333.15	0.8176	988.6
333.15	0.8956	987.7
333.15	1.0000	986.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-[2-(2-ethoxyethoxy)ethoxy]- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	998.2
293.15	0.0112	1006.9
293.15	0.0249	1016.6
293.15	0.0413	1026.2
293.15	0.0628	1035.1
293.15	0.0918	1040.8
293.15	0.1317	1042.7
293.15	0.1905	1042.2
293.15	0.2885	1038.7
293.15	0.4019	1033.6
293.15	0.4747	1031.1
293.15	0.6076	1027.3
293.15	0.7399	1024.4
293.15	0.8176	1022.9
293.15	0.8956	1021.8
293.15	1.0000	1020.6
298.15	1.0000	1016.3
303.15	0.0000	995.7
303.15	0.0112	1003.7
303.15	0.0249	1012.6
303.15	0.0413	1020.7
303.15	0.0628	1028.7
303.15	0.0918	1032.8
303.15	0.1317	1034.9
303.15	0.1905	1033.9
303.15	0.2885	1029.8
303.15	0.4019	1024.9
303.15	0.4747	1022.3
303.15	0.6076	1018.5
303.15	0.7399	1015.5
303.15	0.8176	1014.1
303.15	0.8956	1013.1
303.15	1.0000	1011.9
308.15	1.0000	1008.1
313.15	0.0000	992.2
313.15	0.0112	999.7
313.15	0.0249	1007.5
313.15	0.0413	1014.8
313.15	0.0628	1021.8
313.15	0.0918	1025.3
313.15	0.1317	1026.5
313.15	0.1905	1025.5
313.15	0.2885	1021.4
313.15	0.4019	1016.5
313.15	0.4747	1013.9
313.15	0.6076	1010.2
313.15	0.7399	1007.4
313.15	0.8176	1006.1
313.15	0.8956	1005.1
313.15	1.0000	1003.9
323.15	0.0000	988.1
323.15	0.0112	995.1
323.15	0.0249	1002.1
323.15	0.0413	1008.7
323.15	0.0628	1014.4
323.15	0.0918	1017.4
323.15	0.1317	1018.1
323.15	0.1905	1016.8
323.15	0.2885	1012.7
323.15	0.4019	1007.7
323.15	0.4747	1005.2
323.15	0.6076	1001.6
323.15	0.7399	998.8
323.15	0.8176	997.6
323.15	0.8956	996.6
323.15	1.0000	995.5
333.15	0.0000	983.2
333.15	0.0112	989.6
333.15	0.0249	995.7
333.15	0.0413	1001.9
333.15	0.0628	1006.2
333.15	0.0918	1008.5
333.15	0.1317	1008.7
333.15	0.1905	1007.3
333.15	0.2885	1003.1
333.15	0.4019	998.5
333.15	0.4747	996.1
333.15	0.6076	992.5
333.15	0.7399	989.8
333.15	0.8176	988.6
333.15	0.8956	987.7
333.15	1.0000	986.7

Sources

• Density and Viscosity of the Binary Mixture of Triethylene Glycol Monoethyl Ether + Water from (293.15 to 333.15) K at Atmospheric Pressure