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

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	0.0050
293.15	0.0515	0.0044
293.15	0.1039	0.0041
293.15	0.1456	0.0039
293.15	0.2078	0.0037
293.15	0.2501	0.0036
293.15	0.3127	0.0035
293.15	0.3517	0.0034
293.15	0.5241	0.0033
293.15	0.6227	0.0033
293.15	0.7217	0.0034
293.15	0.8227	0.0034
293.15	0.9150	0.0036
293.15	1.0000	0.0036
298.15	0.0000	0.0044
298.15	0.0515	0.0039
298.15	0.1039	0.0037
298.15	0.1456	0.0035
298.15	0.2078	0.0034
298.15	0.2501	0.0032
298.15	0.3127	0.0031
298.15	0.3517	0.0031
298.15	0.5241	0.0030
298.15	0.6227	0.0030
298.15	0.7217	0.0030
298.15	0.8227	0.0031
298.15	0.9150	0.0032
298.15	1.0000	0.0033
303.15	0.0000	0.0037
303.15	0.0515	0.0034
303.15	0.1039	0.0032
303.15	0.1456	0.0030
303.15	0.2078	0.0029
303.15	0.2501	0.0028
303.15	0.3127	0.0027
303.15	0.3517	0.0027
303.15	0.5241	0.0026
303.15	0.6227	0.0026
303.15	0.7217	0.0026
303.15	0.8227	0.0027
303.15	0.9150	0.0028
303.15	1.0000	0.0029
308.15	0.0000	0.0031
308.15	0.0515	0.0029
308.15	0.1039	0.0027
308.15	0.1456	0.0026
308.15	0.2078	0.0025
308.15	0.2501	0.0024
308.15	0.3127	0.0024
308.15	0.3517	0.0023
308.15	0.5241	0.0023
308.15	0.6227	0.0023
308.15	0.7217	0.0023
308.15	0.8227	0.0023
308.15	0.9150	0.0024
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	0.0050
293.15	0.0515	0.0044
293.15	0.1039	0.0041
293.15	0.1456	0.0039
293.15	0.2078	0.0037
293.15	0.2501	0.0036
293.15	0.3127	0.0035
293.15	0.3517	0.0034
293.15	0.5241	0.0033
293.15	0.6227	0.0033
293.15	0.7217	0.0034
293.15	0.8227	0.0034
293.15	0.9150	0.0036
293.15	1.0000	0.0036
298.15	0.0000	0.0044
298.15	0.0515	0.0039
298.15	0.1039	0.0037
298.15	0.1456	0.0035
298.15	0.2078	0.0034
298.15	0.2501	0.0032
298.15	0.3127	0.0031
298.15	0.3517	0.0031
298.15	0.5241	0.0030
298.15	0.6227	0.0030
298.15	0.7217	0.0030
298.15	0.8227	0.0031
298.15	0.9150	0.0032
298.15	1.0000	0.0033
303.15	0.0000	0.0037
303.15	0.0515	0.0034
303.15	0.1039	0.0032
303.15	0.1456	0.0030
303.15	0.2078	0.0029
303.15	0.2501	0.0028
303.15	0.3127	0.0027
303.15	0.3517	0.0027
303.15	0.5241	0.0026
303.15	0.6227	0.0026
303.15	0.7217	0.0026
303.15	0.8227	0.0027
303.15	0.9150	0.0028
303.15	1.0000	0.0029
308.15	0.0000	0.0031
308.15	0.0515	0.0029
308.15	0.1039	0.0027
308.15	0.1456	0.0026
308.15	0.2078	0.0025
308.15	0.2501	0.0024
308.15	0.3127	0.0024
308.15	0.3517	0.0023
308.15	0.5241	0.0023
308.15	0.6227	0.0023
308.15	0.7217	0.0023
308.15	0.8227	0.0023
308.15	0.9150	0.0024
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	0.0515	828.146
293.15	0.1039	837.651
293.15	0.1456	845.454
293.15	0.2078	857.041
293.15	0.2501	864.989
293.15	0.3127	876.967
293.15	0.3517	884.493
293.15	0.5241	918.471
293.15	0.6227	938.481
293.15	0.7217	959.157
293.15	0.8227	980.826
293.15	0.9150	1000.908
298.15	0.0515	824.518
298.15	0.1039	833.976
298.15	0.1456	841.738
298.15	0.2078	853.267
298.15	0.2501	861.179
298.15	0.3127	873.107
298.15	0.3517	880.591
298.15	0.5241	914.427
298.15	0.6227	934.36
298.15	0.7217	954.955
298.15	0.8227	976.55
298.15	0.9150	996.56
303.15	0.0515	820.874
303.15	0.1039	830.282
303.15	0.1456	838.004
303.15	0.2078	849.482
303.15	0.2501	857.352
303.15	0.3127	869.225
303.15	0.3517	876.678
303.15	0.5241	910.37
303.15	0.6227	930.226
303.15	0.7217	950.745
303.15	0.8227	972.261
303.15	0.9150	992.202
308.15	0.0515	817.198
308.15	0.1039	826.564
308.15	0.1456	834.246
308.15	0.2078	845.669
308.15	0.2501	853.504
308.15	0.3127	865.322
308.15	0.3517	872.742
308.15	0.5241	906.299
308.15	0.6227	926.073
308.15	0.7217	946.516
308.15	0.8227	967.953
308.15	0.9150	987.826

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	0.0515	828.146
293.15	0.1039	837.651
293.15	0.1456	845.454
293.15	0.2078	857.041
293.15	0.2501	864.989
293.15	0.3127	876.967
293.15	0.3517	884.493
293.15	0.5241	918.471
293.15	0.6227	938.481
293.15	0.7217	959.157
293.15	0.8227	980.826
293.15	0.9150	1000.908
298.15	0.0515	824.518
298.15	0.1039	833.976
298.15	0.1456	841.738
298.15	0.2078	853.267
298.15	0.2501	861.179
298.15	0.3127	873.107
298.15	0.3517	880.591
298.15	0.5241	914.427
298.15	0.6227	934.36
298.15	0.7217	954.955
298.15	0.8227	976.55
298.15	0.9150	996.56
303.15	0.0515	820.874
303.15	0.1039	830.282
303.15	0.1456	838.004
303.15	0.2078	849.482
303.15	0.2501	857.352
303.15	0.3127	869.225
303.15	0.3517	876.678
303.15	0.5241	910.37
303.15	0.6227	930.226
303.15	0.7217	950.745
303.15	0.8227	972.261
303.15	0.9150	992.202
308.15	0.0515	817.198
308.15	0.1039	826.564
308.15	0.1456	834.246
308.15	0.2078	845.669
308.15	0.2501	853.504
308.15	0.3127	865.322
308.15	0.3517	872.742
308.15	0.5241	906.299
308.15	0.6227	926.073
308.15	0.7217	946.516
308.15	0.8227	967.953
308.15	0.9150	987.826

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	0.0515	1322.4
293.15	0.1039	1324.9
293.15	0.1456	1327.5
293.15	0.2078	1331.1
293.15	0.2501	1334.2
293.15	0.3127	1338.7
293.15	0.3517	1342.1
293.15	0.5241	1358.7
293.15	0.6227	1370.5
293.15	0.7217	1384.3
293.15	0.8227	1400.4
293.15	0.9150	1416.4
298.15	0.0515	1305.4
298.15	0.1039	1308.0
298.15	0.1456	1310.6
298.15	0.2078	1314.3
298.15	0.2501	1317.4
298.15	0.3127	1322.0
298.15	0.3517	1325.3
298.15	0.5241	1341.9
298.15	0.6227	1353.8
298.15	0.7217	1367.5
298.15	0.8227	1383.5
298.15	0.9150	1399.5
303.15	0.0515	1288.7
303.15	0.1039	1291.3
303.15	0.1456	1293.9
303.15	0.2078	1297.6
303.15	0.2501	1300.7
303.15	0.3127	1305.3
303.15	0.3517	1308.7
303.15	0.5241	1325.3
303.15	0.6227	1337.1
303.15	0.7217	1350.8
303.15	0.8227	1366.7
303.15	0.9150	1382.6
308.15	0.0515	1272.1
308.15	0.1039	1274.7
308.15	0.1456	1277.3
308.15	0.2078	1280.0
308.15	0.2501	1284.2
308.15	0.3127	1288.8
308.15	0.3517	1292.1
308.15	0.5241	1308.8
308.15	0.6227	1320.6
308.15	0.7217	1334.2
308.15	0.8227	1350.0
308.15	0.9150	1365.8

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	0.0515	1322.4
293.15	0.1039	1324.9
293.15	0.1456	1327.5
293.15	0.2078	1331.1
293.15	0.2501	1334.2
293.15	0.3127	1338.7
293.15	0.3517	1342.1
293.15	0.5241	1358.7
293.15	0.6227	1370.5
293.15	0.7217	1384.3
293.15	0.8227	1400.4
293.15	0.9150	1416.4
298.15	0.0515	1305.4
298.15	0.1039	1308.0
298.15	0.1456	1310.6
298.15	0.2078	1314.3
298.15	0.2501	1317.4
298.15	0.3127	1322.0
298.15	0.3517	1325.3
298.15	0.5241	1341.9
298.15	0.6227	1353.8
298.15	0.7217	1367.5
298.15	0.8227	1383.5
298.15	0.9150	1399.5
303.15	0.0515	1288.7
303.15	0.1039	1291.3
303.15	0.1456	1293.9
303.15	0.2078	1297.6
303.15	0.2501	1300.7
303.15	0.3127	1305.3
303.15	0.3517	1308.7
303.15	0.5241	1325.3
303.15	0.6227	1337.1
303.15	0.7217	1350.8
303.15	0.8227	1366.7
303.15	0.9150	1382.6
308.15	0.0515	1272.1
308.15	0.1039	1274.7
308.15	0.1456	1277.3
308.15	0.2078	1280.0
308.15	0.2501	1284.2
308.15	0.3127	1288.8
308.15	0.3517	1292.1
308.15	0.5241	1308.8
308.15	0.6227	1320.6
308.15	0.7217	1334.2
308.15	0.8227	1350.0
308.15	0.9150	1365.8

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	0.0515	7.5300e-08
293.15	0.1039	1.5380e-07
293.15	0.1456	1.8410e-07
293.15	0.2078	2.4700e-07
293.15	0.2501	2.8580e-07
293.15	0.3127	3.2140e-07
293.15	0.3517	3.4030e-07
293.15	0.5241	3.7970e-07
293.15	0.6227	3.6580e-07
293.15	0.7217	3.0810e-07
293.15	0.8227	2.1190e-07
293.15	0.9150	1.2110e-07
298.15	0.0515	7.7400e-08
298.15	0.1039	1.5640e-07
298.15	0.1456	1.8880e-07
298.15	0.2078	2.5330e-07
298.15	0.2501	2.9260e-07
298.15	0.3127	3.2820e-07
298.15	0.3517	3.4860e-07
298.15	0.5241	3.8780e-07
298.15	0.6227	3.7280e-07
298.15	0.7217	3.1400e-07
298.15	0.8227	2.1500e-07
298.15	0.9150	1.2260e-07
303.15	0.0515	7.8100e-08
303.15	0.1039	1.5890e-07
303.15	0.1456	1.9280e-07
303.15	0.2078	2.5800e-07
303.15	0.2501	2.9880e-07
303.15	0.3127	3.3540e-07
303.15	0.3517	3.5590e-07
303.15	0.5241	3.9570e-07
303.15	0.6227	3.7990e-07
303.15	0.7217	3.1980e-07
303.15	0.8227	2.1930e-07
303.15	0.9150	1.2480e-07
308.15	0.0515	8.0400e-08
308.15	0.1039	1.6200e-07
308.15	0.1456	1.9710e-07
308.15	0.2078	2.6350e-07
308.15	0.2501	3.0470e-07
308.15	0.3127	3.4220e-07
308.15	0.3517	3.6290e-07
308.15	0.5241	4.0180e-07
308.15	0.6227	3.8570e-07
308.15	0.7217	3.2390e-07
308.15	0.8227	2.2160e-07
308.15	0.9150	1.2480e-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	0.0515	7.5300e-08
293.15	0.1039	1.5380e-07
293.15	0.1456	1.8410e-07
293.15	0.2078	2.4700e-07
293.15	0.2501	2.8580e-07
293.15	0.3127	3.2140e-07
293.15	0.3517	3.4030e-07
293.15	0.5241	3.7970e-07
293.15	0.6227	3.6580e-07
293.15	0.7217	3.0810e-07
293.15	0.8227	2.1190e-07
293.15	0.9150	1.2110e-07
298.15	0.0515	7.7400e-08
298.15	0.1039	1.5640e-07
298.15	0.1456	1.8880e-07
298.15	0.2078	2.5330e-07
298.15	0.2501	2.9260e-07
298.15	0.3127	3.2820e-07
298.15	0.3517	3.4860e-07
298.15	0.5241	3.8780e-07
298.15	0.6227	3.7280e-07
298.15	0.7217	3.1400e-07
298.15	0.8227	2.1500e-07
298.15	0.9150	1.2260e-07
303.15	0.0515	7.8100e-08
303.15	0.1039	1.5890e-07
303.15	0.1456	1.9280e-07
303.15	0.2078	2.5800e-07
303.15	0.2501	2.9880e-07
303.15	0.3127	3.3540e-07
303.15	0.3517	3.5590e-07
303.15	0.5241	3.9570e-07
303.15	0.6227	3.7990e-07
303.15	0.7217	3.1980e-07
303.15	0.8227	2.1930e-07
303.15	0.9150	1.2480e-07
308.15	0.0515	8.0400e-08
308.15	0.1039	1.6200e-07
308.15	0.1456	1.9710e-07
308.15	0.2078	2.6350e-07
308.15	0.2501	3.0470e-07
308.15	0.3127	3.4220e-07
308.15	0.3517	3.6290e-07
308.15	0.5241	4.0180e-07
308.15	0.6227	3.8570e-07
308.15	0.7217	3.2390e-07
308.15	0.8227	2.2160e-07
308.15	0.9150	1.2480e-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