Mixture of Ethanol, 2-(2-ethoxyethoxy)- + 1-Octanol

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)
3. c_sound,fluid - Speed of Sound, m/s (2)
4. Excess molar volume, m3/mol (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0083
293.15	0.0518	0.0075
293.15	0.1011	0.0069
293.15	0.1625	0.0062
293.15	0.1944	0.0059
293.15	0.2538	0.0059
293.15	0.3165	0.0051
293.15	0.3685	0.0048
293.15	0.4975	0.0044
293.15	0.6048	0.0041
293.15	0.7202	0.0038
293.15	0.8165	0.0037
293.15	0.9144	0.0037
293.15	1.0000	0.0036
298.15	0.0000	0.0071
298.15	0.0518	0.0062
298.15	0.1011	0.0060
298.15	0.1625	0.0054
298.15	0.1944	0.0052
298.15	0.2538	0.0048
298.15	0.3165	0.0045
298.15	0.3685	0.0043
298.15	0.4975	0.0039
298.15	0.6048	0.0036
298.15	0.7202	0.0034
298.15	0.8165	0.0033
298.15	0.9144	0.0033
298.15	1.0000	0.0033
303.15	0.0000	0.0060
303.15	0.0518	0.0054
303.15	0.1011	0.0050
303.15	0.1625	0.0046
303.15	0.1944	0.0044
303.15	0.2538	0.0043
303.15	0.3165	0.0038
303.15	0.3685	0.0037
303.15	0.4975	0.0034
303.15	0.6048	0.0031
303.15	0.7202	0.0030
303.15	0.8165	0.0029
303.15	0.9144	0.0028
303.15	1.0000	0.0029
308.15	0.0000	0.0050
308.15	0.0518	0.0045
308.15	0.1011	0.0042
308.15	0.1625	0.0039
308.15	0.1944	0.0038
308.15	0.2538	0.0035
308.15	0.3165	0.0033
308.15	0.3685	0.0032
308.15	0.4975	0.0029
308.15	0.6048	0.0027
308.15	0.7202	0.0026
308.15	0.8165	0.0025
308.15	0.9144	0.0025
308.15	1.0000	0.0025

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0083
293.15	0.0518	0.0075
293.15	0.1011	0.0069
293.15	0.1625	0.0062
293.15	0.1944	0.0059
293.15	0.2538	0.0059
293.15	0.3165	0.0051
293.15	0.3685	0.0048
293.15	0.4975	0.0044
293.15	0.6048	0.0041
293.15	0.7202	0.0038
293.15	0.8165	0.0037
293.15	0.9144	0.0037
293.15	1.0000	0.0036
298.15	0.0000	0.0071
298.15	0.0518	0.0062
298.15	0.1011	0.0060
298.15	0.1625	0.0054
298.15	0.1944	0.0052
298.15	0.2538	0.0048
298.15	0.3165	0.0045
298.15	0.3685	0.0043
298.15	0.4975	0.0039
298.15	0.6048	0.0036
298.15	0.7202	0.0034
298.15	0.8165	0.0033
298.15	0.9144	0.0033
298.15	1.0000	0.0033
303.15	0.0000	0.0060
303.15	0.0518	0.0054
303.15	0.1011	0.0050
303.15	0.1625	0.0046
303.15	0.1944	0.0044
303.15	0.2538	0.0043
303.15	0.3165	0.0038
303.15	0.3685	0.0037
303.15	0.4975	0.0034
303.15	0.6048	0.0031
303.15	0.7202	0.0030
303.15	0.8165	0.0029
303.15	0.9144	0.0028
303.15	1.0000	0.0029
308.15	0.0000	0.0050
308.15	0.0518	0.0045
308.15	0.1011	0.0042
308.15	0.1625	0.0039
308.15	0.1944	0.0038
308.15	0.2538	0.0035
308.15	0.3165	0.0033
308.15	0.3685	0.0032
308.15	0.4975	0.0029
308.15	0.6048	0.0027
308.15	0.7202	0.0026
308.15	0.8165	0.0025
308.15	0.9144	0.0025
308.15	1.0000	0.0025

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0518	832.339
293.15	0.1011	839.204
293.15	0.1625	848.155
293.15	0.1944	853.018
293.15	0.2538	862.076
293.15	0.3165	872.254
293.15	0.3685	880.933
293.15	0.4975	904.111
293.15	0.6048	925.139
293.15	0.7202	949.653
293.15	0.8165	971.878
293.15	0.9144	996.047
298.15	0.0518	828.835
298.15	0.1011	835.659
298.15	0.1625	844.559
298.15	0.1944	849.396
298.15	0.2538	858.398
298.15	0.3165	868.522
298.15	0.3685	877.154
298.15	0.4975	900.211
298.15	0.6048	921.137
298.15	0.7202	945.535
298.15	0.8165	991.74
298.15	0.9144	938.234
303.15	0.0518	825.317
303.15	0.1011	832.097
303.15	0.1625	840.951
303.15	0.1944	845.762
303.15	0.2538	854.713
303.15	0.3165	864.78
303.15	0.3685	873.364
303.15	0.4975	896.3
303.15	0.6048	917.122
303.15	0.7202	941.409
303.15	0.8165	963.444
303.15	0.9144	987.41
308.15	0.0518	821.777
308.15	0.1011	828.522
308.15	0.1625	837.324
308.15	0.1944	842.106
308.15	0.2538	851.006
308.15	0.3165	861.019
308.15	0.3685	869.558
308.15	0.4975	892.371
308.15	0.6048	913.092
308.15	0.7202	937.267
308.15	0.8165	959.204
308.15	0.9144	983.069

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0518	832.339
293.15	0.1011	839.204
293.15	0.1625	848.155
293.15	0.1944	853.018
293.15	0.2538	862.076
293.15	0.3165	872.254
293.15	0.3685	880.933
293.15	0.4975	904.111
293.15	0.6048	925.139
293.15	0.7202	949.653
293.15	0.8165	971.878
293.15	0.9144	996.047
298.15	0.0518	828.835
298.15	0.1011	835.659
298.15	0.1625	844.559
298.15	0.1944	849.396
298.15	0.2538	858.398
298.15	0.3165	868.522
298.15	0.3685	877.154
298.15	0.4975	900.211
298.15	0.6048	921.137
298.15	0.7202	945.535
298.15	0.8165	991.74
298.15	0.9144	938.234
303.15	0.0518	825.317
303.15	0.1011	832.097
303.15	0.1625	840.951
303.15	0.1944	845.762
303.15	0.2538	854.713
303.15	0.3165	864.78
303.15	0.3685	873.364
303.15	0.4975	896.3
303.15	0.6048	917.122
303.15	0.7202	941.409
303.15	0.8165	963.444
303.15	0.9144	987.41
308.15	0.0518	821.777
308.15	0.1011	828.522
308.15	0.1625	837.324
308.15	0.1944	842.106
308.15	0.2538	851.006
308.15	0.3165	861.019
308.15	0.3685	869.558
308.15	0.4975	892.371
308.15	0.6048	913.092
308.15	0.7202	937.267
308.15	0.8165	959.204
308.15	0.9144	983.069

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0518	1364.1
293.15	0.1011	1363.5
293.15	0.1625	1363.1
293.15	0.1944	1363.7
293.15	0.2538	1364.5
293.15	0.3165	1365.7
293.15	0.3685	1370.8
293.15	0.4975	1377.4
293.15	0.6048	1387.7
293.15	0.7202	1399.5
293.15	0.8165	1415.1
293.15	0.9144	1349.4
298.15	0.0518	1347.1
298.15	0.1011	1346.5
298.15	0.1625	1346.3
298.15	0.1944	1346.7
298.15	0.2538	1347.6
298.15	0.3165	1348.9
298.15	0.3685	1354.1
298.15	0.4975	1360.7
298.15	0.6048	1370.9
298.15	0.7202	1382.7
298.15	0.8165	1398.2
298.15	0.9144	1332.2
303.15	0.0518	1330.3
303.15	0.1011	1329.8
303.15	0.1625	1329.5
303.15	0.1944	1329.6
303.15	0.2538	1330.1
303.15	0.3165	1330.9
303.15	0.3685	1332.3
303.15	0.4975	1337.5
303.15	0.6048	1343.9
303.15	0.7202	1354.3
303.15	0.8165	1381.3
303.15	0.9144	1315.0
308.15	0.0518	1313.7
308.15	0.1011	1313.2
308.15	0.1625	1312.9
308.15	0.1944	1312.9
308.15	0.2538	1313.5
308.15	0.3165	1314.5
308.15	0.3685	1315.7
308.15	0.4975	1320.9
308.15	0.6048	1327.4
308.15	0.7202	1337.7
308.15	0.8165	1349.3
308.15	0.9144	1364.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0518	1364.1
293.15	0.1011	1363.5
293.15	0.1625	1363.1
293.15	0.1944	1363.7
293.15	0.2538	1364.5
293.15	0.3165	1365.7
293.15	0.3685	1370.8
293.15	0.4975	1377.4
293.15	0.6048	1387.7
293.15	0.7202	1399.5
293.15	0.8165	1415.1
293.15	0.9144	1349.4
298.15	0.0518	1347.1
298.15	0.1011	1346.5
298.15	0.1625	1346.3
298.15	0.1944	1346.7
298.15	0.2538	1347.6
298.15	0.3165	1348.9
298.15	0.3685	1354.1
298.15	0.4975	1360.7
298.15	0.6048	1370.9
298.15	0.7202	1382.7
298.15	0.8165	1398.2
298.15	0.9144	1332.2
303.15	0.0518	1330.3
303.15	0.1011	1329.8
303.15	0.1625	1329.5
303.15	0.1944	1329.6
303.15	0.2538	1330.1
303.15	0.3165	1330.9
303.15	0.3685	1332.3
303.15	0.4975	1337.5
303.15	0.6048	1343.9
303.15	0.7202	1354.3
303.15	0.8165	1381.3
303.15	0.9144	1315.0
308.15	0.0518	1313.7
308.15	0.1011	1313.2
308.15	0.1625	1312.9
308.15	0.1944	1312.9
308.15	0.2538	1313.5
308.15	0.3165	1314.5
308.15	0.3685	1315.7
308.15	0.4975	1320.9
308.15	0.6048	1327.4
308.15	0.7202	1337.7
308.15	0.8165	1349.3
308.15	0.9144	1364.5

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid	Excess molar volume, m3/mol - Liquid
293.15	0.0518	1.0220e-07
293.15	0.1011	2.0750e-07
293.15	0.1625	3.0920e-07
293.15	0.1944	3.4410e-07
293.15	0.2538	4.4580e-07
293.15	0.3165	5.0150e-07
293.15	0.3685	5.5180e-07
293.15	0.4975	5.9250e-07
293.15	0.6048	5.6810e-07
293.15	0.7202	4.9620e-07
293.15	0.8165	3.8870e-07
293.15	0.9144	2.6860e-07
298.15	0.0518	1.0390e-07
298.15	0.1011	2.1110e-07
298.15	0.1625	3.1450e-07
298.15	0.1944	3.4990e-07
298.15	0.2538	4.5400e-07
298.15	0.3165	5.1050e-07
298.15	0.3685	5.6170e-07
298.15	0.4975	6.0330e-07
298.15	0.6048	5.7810e-07
298.15	0.7202	5.0480e-07
298.15	0.8165	3.9460e-07
298.15	0.9144	2.7050e-07
303.15	0.0518	1.0440e-07
303.15	0.1011	2.1420e-07
303.15	0.1625	3.1860e-07
303.15	0.1944	3.5470e-07
303.15	0.2538	4.6060e-07
303.15	0.3165	5.1860e-07
303.15	0.3685	5.7090e-07
303.15	0.4975	6.1390e-07
303.15	0.6048	5.8870e-07
303.15	0.7202	5.1360e-07
303.15	0.8165	4.0090e-07
303.15	0.9144	2.7480e-07
308.15	0.0518	1.0660e-07
308.15	0.1011	2.1720e-07
308.15	0.1625	3.2370e-07
308.15	0.1944	3.6090e-07
308.15	0.2538	4.6840e-07
308.15	0.3165	5.2740e-07
308.15	0.3685	5.8040e-07
308.15	0.4975	6.2480e-07
308.15	0.6048	5.9880e-07
308.15	0.7202	5.2190e-07
308.15	0.8165	4.0690e-07
308.15	0.9144	2.7790e-07

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid	Excess molar volume, m3/mol - Liquid
293.15	0.0518	1.0220e-07
293.15	0.1011	2.0750e-07
293.15	0.1625	3.0920e-07
293.15	0.1944	3.4410e-07
293.15	0.2538	4.4580e-07
293.15	0.3165	5.0150e-07
293.15	0.3685	5.5180e-07
293.15	0.4975	5.9250e-07
293.15	0.6048	5.6810e-07
293.15	0.7202	4.9620e-07
293.15	0.8165	3.8870e-07
293.15	0.9144	2.6860e-07
298.15	0.0518	1.0390e-07
298.15	0.1011	2.1110e-07
298.15	0.1625	3.1450e-07
298.15	0.1944	3.4990e-07
298.15	0.2538	4.5400e-07
298.15	0.3165	5.1050e-07
298.15	0.3685	5.6170e-07
298.15	0.4975	6.0330e-07
298.15	0.6048	5.7810e-07
298.15	0.7202	5.0480e-07
298.15	0.8165	3.9460e-07
298.15	0.9144	2.7050e-07
303.15	0.0518	1.0440e-07
303.15	0.1011	2.1420e-07
303.15	0.1625	3.1860e-07
303.15	0.1944	3.5470e-07
303.15	0.2538	4.6060e-07
303.15	0.3165	5.1860e-07
303.15	0.3685	5.7090e-07
303.15	0.4975	6.1390e-07
303.15	0.6048	5.8870e-07
303.15	0.7202	5.1360e-07
303.15	0.8165	4.0090e-07
303.15	0.9144	2.7480e-07
308.15	0.0518	1.0660e-07
308.15	0.1011	2.1720e-07
308.15	0.1625	3.2370e-07
308.15	0.1944	3.6090e-07
308.15	0.2538	4.6840e-07
308.15	0.3165	5.2740e-07
308.15	0.3685	5.8040e-07
308.15	0.4975	6.2480e-07
308.15	0.6048	5.9880e-07
308.15	0.7202	5.2190e-07
308.15	0.8165	4.0690e-07
308.15	0.9144	2.7790e-07

Sources

• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of diethylene glycol monomethyl ether with 1-alkanols at temperatures from (293.15 to 308.15) K