Mixture of 1-Hexanol + Ethylenediamine

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 Ethylenediamine (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0773	0.0043
298.15	0.1213	0.0042
298.15	0.1604	0.0041
298.15	0.1925	0.0040
298.15	0.2525	0.0038
298.15	0.2907	0.0037
298.15	0.3942	0.0034
298.15	0.5086	0.0029
298.15	0.6059	0.0025
298.15	0.7125	0.0021
298.15	0.8100	0.0019
298.15	0.8583	0.0017
298.15	0.9028	0.0016
298.15	0.9450	0.0015
303.15	0.0773	0.0036
303.15	0.1213	0.0036
303.15	0.1604	0.0035
303.15	0.1925	0.0035
303.15	0.2525	0.0033
303.15	0.2907	0.0032
303.15	0.3942	0.0029
303.15	0.5086	0.0025
303.15	0.6059	0.0022
303.15	0.7125	0.0019
303.15	0.8100	0.0016
303.15	0.8583	0.0015
303.15	0.9028	0.0014
303.15	0.9450	0.0013
308.15	0.0773	0.0031
308.15	0.1213	0.0030
308.15	0.1604	0.0030
308.15	0.1925	0.0029
308.15	0.2525	0.0028
308.15	0.2907	0.0027
308.15	0.3942	0.0025
308.15	0.5086	0.0022
308.15	0.6059	0.0019
308.15	0.7125	0.0016
308.15	0.8100	0.0014
308.15	0.8583	0.0013
308.15	0.9028	0.0012
308.15	0.9450	0.0012

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylenediamine (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0773	0.0043
298.15	0.1213	0.0042
298.15	0.1604	0.0041
298.15	0.1925	0.0040
298.15	0.2525	0.0038
298.15	0.2907	0.0037
298.15	0.3942	0.0034
298.15	0.5086	0.0029
298.15	0.6059	0.0025
298.15	0.7125	0.0021
298.15	0.8100	0.0019
298.15	0.8583	0.0017
298.15	0.9028	0.0016
298.15	0.9450	0.0015
303.15	0.0773	0.0036
303.15	0.1213	0.0036
303.15	0.1604	0.0035
303.15	0.1925	0.0035
303.15	0.2525	0.0033
303.15	0.2907	0.0032
303.15	0.3942	0.0029
303.15	0.5086	0.0025
303.15	0.6059	0.0022
303.15	0.7125	0.0019
303.15	0.8100	0.0016
303.15	0.8583	0.0015
303.15	0.9028	0.0014
303.15	0.9450	0.0013
308.15	0.0773	0.0031
308.15	0.1213	0.0030
308.15	0.1604	0.0030
308.15	0.1925	0.0029
308.15	0.2525	0.0028
308.15	0.2907	0.0027
308.15	0.3942	0.0025
308.15	0.5086	0.0022
308.15	0.6059	0.0019
308.15	0.7125	0.0016
308.15	0.8100	0.0014
308.15	0.8583	0.0013
308.15	0.9028	0.0012
308.15	0.9450	0.0012

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylenediamine (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0773	824.126
293.15	0.1231	827.205
293.15	0.1604	829.772
293.15	0.1925	831.826
293.15	0.2525	835.69
293.15	0.2907	837.925
293.15	0.3942	844.247
293.15	0.5086	851.229
293.15	0.6059	857.577
293.15	0.7125	865.791
293.15	0.8100	874.361
293.15	0.8583	879.425
293.15	0.9028	884.825
293.15	0.9450	890.109
298.15	0.0773	820.463
298.15	0.1231	823.489
298.15	0.1604	826.005
298.15	0.1925	828.015
298.15	0.2525	831.807
298.15	0.2907	833.999
298.15	0.3942	840.22
298.15	0.5086	847.107
298.15	0.6059	853.36
298.15	0.7125	861.471
298.15	0.8100	869.926
298.15	0.8583	874.936
298.15	0.9028	880.277
298.15	0.9450	885.496
303.15	0.0773	816.783
303.15	0.1213	819.755
303.15	0.1604	822.223
303.15	0.1925	824.193
303.15	0.2525	827.911
303.15	0.2907	830.062
303.15	0.3942	836.182
303.15	0.5086	842.967
303.15	0.6059	849.135
303.15	0.7125	857.138
303.15	0.8100	865.482
303.15	0.8583	870.432
303.15	0.9028	875.713
303.15	0.9450	880.874
308.15	0.0773	813.087
308.15	0.1213	816.005
308.15	0.1604	818.427
308.15	0.1925	820.356
308.15	0.2525	824.0
308.15	0.2907	826.113
308.15	0.3942	832.134
308.15	0.5086	838.821
308.15	0.6059	844.903
308.15	0.7125	852.798
308.15	0.8100	861.03
308.15	0.8583	865.917
308.15	0.9028	871.143
308.15	0.9450	876.241
313.15	0.0773	809.362
313.15	0.1213	812.228
313.15	0.1604	814.602
313.15	0.1925	816.496
313.15	0.2525	820.069
313.15	0.2907	822.144
313.15	0.3942	828.065
313.15	0.5086	834.657
313.15	0.6059	840.646
313.15	0.7125	848.435
313.15	0.8100	856.554
313.15	0.8583	861.384
313.15	0.9028	866.55
313.15	0.9450	871.587

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylenediamine (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0773	824.126
293.15	0.1231	827.205
293.15	0.1604	829.772
293.15	0.1925	831.826
293.15	0.2525	835.69
293.15	0.2907	837.925
293.15	0.3942	844.247
293.15	0.5086	851.229
293.15	0.6059	857.577
293.15	0.7125	865.791
293.15	0.8100	874.361
293.15	0.8583	879.425
293.15	0.9028	884.825
293.15	0.9450	890.109
298.15	0.0773	820.463
298.15	0.1231	823.489
298.15	0.1604	826.005
298.15	0.1925	828.015
298.15	0.2525	831.807
298.15	0.2907	833.999
298.15	0.3942	840.22
298.15	0.5086	847.107
298.15	0.6059	853.36
298.15	0.7125	861.471
298.15	0.8100	869.926
298.15	0.8583	874.936
298.15	0.9028	880.277
298.15	0.9450	885.496
303.15	0.0773	816.783
303.15	0.1213	819.755
303.15	0.1604	822.223
303.15	0.1925	824.193
303.15	0.2525	827.911
303.15	0.2907	830.062
303.15	0.3942	836.182
303.15	0.5086	842.967
303.15	0.6059	849.135
303.15	0.7125	857.138
303.15	0.8100	865.482
303.15	0.8583	870.432
303.15	0.9028	875.713
303.15	0.9450	880.874
308.15	0.0773	813.087
308.15	0.1213	816.005
308.15	0.1604	818.427
308.15	0.1925	820.356
308.15	0.2525	824.0
308.15	0.2907	826.113
308.15	0.3942	832.134
308.15	0.5086	838.821
308.15	0.6059	844.903
308.15	0.7125	852.798
308.15	0.8100	861.03
308.15	0.8583	865.917
308.15	0.9028	871.143
308.15	0.9450	876.241
313.15	0.0773	809.362
313.15	0.1213	812.228
313.15	0.1604	814.602
313.15	0.1925	816.496
313.15	0.2525	820.069
313.15	0.2907	822.144
313.15	0.3942	828.065
313.15	0.5086	834.657
313.15	0.6059	840.646
313.15	0.7125	848.435
313.15	0.8100	856.554
313.15	0.8583	861.384
313.15	0.9028	866.55
313.15	0.9450	871.587

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylenediamine (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0773	1338.6
293.15	0.1231	1348.9
293.15	0.1604	1358.1
293.15	0.1925	1365.8
293.15	0.2525	1381.0
293.15	0.2907	1390.2
293.15	0.3942	1417.8
293.15	0.5086	1450.5
293.15	0.6059	1482.3
293.15	0.7125	1522.6
293.15	0.8100	1569.0
293.15	0.8583	1596.2
293.15	0.9028	1623.9
293.15	0.9450	1652.7
298.15	0.0773	1321.6
298.15	0.1231	1331.9
298.15	0.1604	1340.9
298.15	0.1925	1348.6
298.15	0.2525	1363.7
298.15	0.2907	1372.7
298.15	0.3942	1399.9
298.15	0.5086	1432.2
298.15	0.6059	1463.5
298.15	0.7125	1503.1
298.15	0.8100	1548.7
298.15	0.8583	1575.4
298.15	0.9028	1602.8
298.15	0.9450	1630.9
303.15	0.0773	1304.6
303.15	0.1213	1314.9
303.15	0.1604	1323.9
303.15	0.1925	1331.5
303.15	0.2525	1346.5
303.15	0.2907	1355.4
303.15	0.3942	1382.2
303.15	0.5086	1413.9
303.15	0.6059	1444.7
303.15	0.7125	1483.7
303.15	0.8100	1528.5
303.15	0.8583	1554.7
303.15	0.9028	1581.5
303.15	0.9450	1609.2
308.15	0.0773	1287.8
308.15	0.1213	1298.2
308.15	0.1604	1307.0
308.15	0.1925	1314.6
308.15	0.2525	1329.3
308.15	0.2907	1338.1
308.15	0.3942	1364.6
308.15	0.5086	1395.8
308.15	0.6059	1426.1
308.15	0.7125	1464.4
308.15	0.8100	1508.5
308.15	0.8583	1534.1
308.15	0.9028	1560.6
308.15	0.9450	1587.7
313.15	0.0773	1271.1
313.15	0.1213	1281.6
313.15	0.1604	1290.4
313.15	0.1925	1297.9
313.15	0.2525	1312.4
313.15	0.2907	1321.1
313.15	0.3942	1347.0
313.15	0.5086	1377.9
313.15	0.6059	1407.5
313.15	0.7125	1445.3
313.15	0.8100	1488.5
313.15	0.8583	1513.6
313.15	0.9028	1539.7
313.15	0.9450	1566.3

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylenediamine (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0773	1338.6
293.15	0.1231	1348.9
293.15	0.1604	1358.1
293.15	0.1925	1365.8
293.15	0.2525	1381.0
293.15	0.2907	1390.2
293.15	0.3942	1417.8
293.15	0.5086	1450.5
293.15	0.6059	1482.3
293.15	0.7125	1522.6
293.15	0.8100	1569.0
293.15	0.8583	1596.2
293.15	0.9028	1623.9
293.15	0.9450	1652.7
298.15	0.0773	1321.6
298.15	0.1231	1331.9
298.15	0.1604	1340.9
298.15	0.1925	1348.6
298.15	0.2525	1363.7
298.15	0.2907	1372.7
298.15	0.3942	1399.9
298.15	0.5086	1432.2
298.15	0.6059	1463.5
298.15	0.7125	1503.1
298.15	0.8100	1548.7
298.15	0.8583	1575.4
298.15	0.9028	1602.8
298.15	0.9450	1630.9
303.15	0.0773	1304.6
303.15	0.1213	1314.9
303.15	0.1604	1323.9
303.15	0.1925	1331.5
303.15	0.2525	1346.5
303.15	0.2907	1355.4
303.15	0.3942	1382.2
303.15	0.5086	1413.9
303.15	0.6059	1444.7
303.15	0.7125	1483.7
303.15	0.8100	1528.5
303.15	0.8583	1554.7
303.15	0.9028	1581.5
303.15	0.9450	1609.2
308.15	0.0773	1287.8
308.15	0.1213	1298.2
308.15	0.1604	1307.0
308.15	0.1925	1314.6
308.15	0.2525	1329.3
308.15	0.2907	1338.1
308.15	0.3942	1364.6
308.15	0.5086	1395.8
308.15	0.6059	1426.1
308.15	0.7125	1464.4
308.15	0.8100	1508.5
308.15	0.8583	1534.1
308.15	0.9028	1560.6
308.15	0.9450	1587.7
313.15	0.0773	1271.1
313.15	0.1213	1281.6
313.15	0.1604	1290.4
313.15	0.1925	1297.9
313.15	0.2525	1312.4
313.15	0.2907	1321.1
313.15	0.3942	1347.0
313.15	0.5086	1377.9
313.15	0.6059	1407.5
313.15	0.7125	1445.3
313.15	0.8100	1488.5
313.15	0.8583	1513.6
313.15	0.9028	1539.7
313.15	0.9450	1566.3

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylenediamine (2) - Liquid	Excess molar volume, m3/mol - Liquid
298.15	0.0773	-2.7970e-07
298.15	0.1231	-4.0950e-07
298.15	0.1604	-5.0820e-07
298.15	0.1925	-5.6090e-07
298.15	0.2525	-6.3750e-07
298.15	0.2907	-6.4050e-07
298.15	0.3942	-6.2160e-07
298.15	0.5086	-4.9710e-07
298.15	0.6059	-3.5080e-07
298.15	0.7125	-2.1960e-07
298.15	0.8100	-9.3700e-08
298.15	0.8583	-6.2800e-08
298.15	0.9028	-6.5800e-08
298.15	0.9450	-5.2700e-08
303.15	0.0773	-2.7620e-07
303.15	0.1231	-4.0390e-07
303.15	0.1604	-5.0000e-07
303.15	0.1925	-5.5040e-07
303.15	0.2525	-6.2450e-07
303.15	0.2907	-6.2620e-07
303.15	0.3942	-6.0660e-07
303.15	0.5086	-4.8400e-07
303.15	0.6059	-3.3860e-07
303.15	0.7125	-2.1040e-07
303.15	0.8100	-8.7600e-08
303.15	0.8583	-5.8100e-08
303.15	0.9028	-6.3100e-08
303.15	0.9450	-5.1300e-08
308.15	0.0773	-2.7420e-07
308.15	0.1213	-3.9940e-07
308.15	0.1604	-4.9320e-07
308.15	0.1925	-5.4180e-07
308.15	0.2525	-6.1290e-07
308.15	0.2907	-6.1340e-07
308.15	0.3942	-5.9290e-07
308.15	0.5086	-4.7120e-07
308.15	0.6059	-3.2770e-07
308.15	0.7125	-2.0180e-07
308.15	0.8100	-8.1300e-08
308.15	0.8583	-5.3400e-08
308.15	0.9028	-6.0300e-08
308.15	0.9450	-5.0200e-08

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylenediamine (2) - Liquid	Excess molar volume, m3/mol - Liquid
298.15	0.0773	-2.7970e-07
298.15	0.1231	-4.0950e-07
298.15	0.1604	-5.0820e-07
298.15	0.1925	-5.6090e-07
298.15	0.2525	-6.3750e-07
298.15	0.2907	-6.4050e-07
298.15	0.3942	-6.2160e-07
298.15	0.5086	-4.9710e-07
298.15	0.6059	-3.5080e-07
298.15	0.7125	-2.1960e-07
298.15	0.8100	-9.3700e-08
298.15	0.8583	-6.2800e-08
298.15	0.9028	-6.5800e-08
298.15	0.9450	-5.2700e-08
303.15	0.0773	-2.7620e-07
303.15	0.1231	-4.0390e-07
303.15	0.1604	-5.0000e-07
303.15	0.1925	-5.5040e-07
303.15	0.2525	-6.2450e-07
303.15	0.2907	-6.2620e-07
303.15	0.3942	-6.0660e-07
303.15	0.5086	-4.8400e-07
303.15	0.6059	-3.3860e-07
303.15	0.7125	-2.1040e-07
303.15	0.8100	-8.7600e-08
303.15	0.8583	-5.8100e-08
303.15	0.9028	-6.3100e-08
303.15	0.9450	-5.1300e-08
308.15	0.0773	-2.7420e-07
308.15	0.1213	-3.9940e-07
308.15	0.1604	-4.9320e-07
308.15	0.1925	-5.4180e-07
308.15	0.2525	-6.1290e-07
308.15	0.2907	-6.1340e-07
308.15	0.3942	-5.9290e-07
308.15	0.5086	-4.7120e-07
308.15	0.6059	-3.2770e-07
308.15	0.7125	-2.0180e-07
308.15	0.8100	-8.1300e-08
308.15	0.8583	-5.3400e-08
308.15	0.9028	-6.0300e-08
308.15	0.9450	-5.0200e-08

Sources

• Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures