Mixture of 1-Octanol + 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	0.0596	0.0069
298.15	0.1021	0.0068
298.15	0.1430	0.0067
298.15	0.2012	0.0065
298.15	0.2633	0.0061
298.15	0.3122	0.0057
298.15	0.4113	0.0050
298.15	0.4919	0.0043
298.15	0.5973	0.0034
298.15	0.7019	0.0027
298.15	0.7938	0.0022
298.15	0.8436	0.0020
298.15	0.8941	0.0018
298.15	0.9546	0.0015
303.15	0.0596	0.0058
303.15	0.1021	0.0057
303.15	0.1430	0.0056
303.15	0.2012	0.0053
303.15	0.2633	0.0050
303.15	0.3122	0.0047
303.15	0.4113	0.0041
303.15	0.4919	0.0036
303.15	0.5973	0.0029
303.15	0.7019	0.0024
303.15	0.7938	0.0020
303.15	0.8436	0.0017
303.15	0.8941	0.0015
303.15	0.9546	0.0013
308.15	0.0596	0.0048
308.15	0.1021	0.0048
308.15	0.1430	0.0047
308.15	0.2012	0.0045
308.15	0.2633	0.0042
308.15	0.3122	0.0040
308.15	0.4113	0.0035
308.15	0.4919	0.0031
308.15	0.5973	0.0025
308.15	0.7019	0.0020
308.15	0.7938	0.0017
308.15	0.8436	0.0015
308.15	0.8941	0.0013
308.15	0.9546	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	0.0596	0.0069
298.15	0.1021	0.0068
298.15	0.1430	0.0067
298.15	0.2012	0.0065
298.15	0.2633	0.0061
298.15	0.3122	0.0057
298.15	0.4113	0.0050
298.15	0.4919	0.0043
298.15	0.5973	0.0034
298.15	0.7019	0.0027
298.15	0.7938	0.0022
298.15	0.8436	0.0020
298.15	0.8941	0.0018
298.15	0.9546	0.0015
303.15	0.0596	0.0058
303.15	0.1021	0.0057
303.15	0.1430	0.0056
303.15	0.2012	0.0053
303.15	0.2633	0.0050
303.15	0.3122	0.0047
303.15	0.4113	0.0041
303.15	0.4919	0.0036
303.15	0.5973	0.0029
303.15	0.7019	0.0024
303.15	0.7938	0.0020
303.15	0.8436	0.0017
303.15	0.8941	0.0015
303.15	0.9546	0.0013
308.15	0.0596	0.0048
308.15	0.1021	0.0048
308.15	0.1430	0.0047
308.15	0.2012	0.0045
308.15	0.2633	0.0042
308.15	0.3122	0.0040
308.15	0.4113	0.0035
308.15	0.4919	0.0031
308.15	0.5973	0.0025
308.15	0.7019	0.0020
308.15	0.7938	0.0017
308.15	0.8436	0.0015
308.15	0.8941	0.0013
308.15	0.9546	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	0.0595	828.135
293.15	0.1021	830.247
293.15	0.1430	832.248
293.15	0.2012	835.047
293.15	0.2633	838.043
293.15	0.3122	839.349
293.15	0.4113	844.656
293.15	0.4919	848.413
293.15	0.5973	854.134
293.15	0.7019	861.054
293.15	0.7938	868.882
293.15	0.8436	874.136
293.15	0.8941	881.269
293.15	0.9546	889.526
298.15	0.0595	824.621
298.15	0.1021	826.683
298.15	0.1430	828.632
298.15	0.2012	831.36
298.15	0.2633	834.276
298.15	0.3122	835.547
298.15	0.4113	840.743
298.15	0.4919	844.426
298.15	0.5973	850.038
298.15	0.7019	856.833
298.15	0.7938	864.539
298.15	0.8436	869.72
298.15	0.8941	876.764
298.15	0.9546	884.925
303.15	0.0595	824.621
303.15	0.1021	826.683
303.15	0.1430	828.632
303.15	0.2012	831.36
303.15	0.2633	834.276
303.15	0.3122	835.547
303.15	0.4113	840.743
303.15	0.4919	844.426
303.15	0.5973	850.038
303.15	0.7019	856.833
303.15	0.7938	864.539
303.15	0.8436	869.72
303.15	0.8941	876.764
303.15	0.9546	884.925
308.15	0.0595	817.544
308.15	0.1021	819.514
308.15	0.1430	821.37
308.15	0.2012	823.957
308.15	0.2633	826.723
308.15	0.3122	827.934
308.15	0.4113	832.902
308.15	0.4919	836.434
308.15	0.5973	841.825
308.15	0.7019	848.372
308.15	0.7938	855.829
308.15	0.8436	860.863
308.15	0.8941	867.723
308.15	0.9546	875.69
313.15	0.0595	813.972
313.15	0.1021	815.903
313.15	0.1430	817.713
313.15	0.2012	820.239
313.15	0.2633	822.931
313.15	0.3122	824.111
313.15	0.4113	828.963
313.15	0.4919	832.42
313.15	0.5973	837.701
313.15	0.7019	844.123
313.15	0.7938	851.455
313.15	0.8436	856.411
313.15	0.8941	863.18
313.15	0.9546	871.049

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	0.0595	828.135
293.15	0.1021	830.247
293.15	0.1430	832.248
293.15	0.2012	835.047
293.15	0.2633	838.043
293.15	0.3122	839.349
293.15	0.4113	844.656
293.15	0.4919	848.413
293.15	0.5973	854.134
293.15	0.7019	861.054
293.15	0.7938	868.882
293.15	0.8436	874.136
293.15	0.8941	881.269
293.15	0.9546	889.526
298.15	0.0595	824.621
298.15	0.1021	826.683
298.15	0.1430	828.632
298.15	0.2012	831.36
298.15	0.2633	834.276
298.15	0.3122	835.547
298.15	0.4113	840.743
298.15	0.4919	844.426
298.15	0.5973	850.038
298.15	0.7019	856.833
298.15	0.7938	864.539
298.15	0.8436	869.72
298.15	0.8941	876.764
298.15	0.9546	884.925
303.15	0.0595	824.621
303.15	0.1021	826.683
303.15	0.1430	828.632
303.15	0.2012	831.36
303.15	0.2633	834.276
303.15	0.3122	835.547
303.15	0.4113	840.743
303.15	0.4919	844.426
303.15	0.5973	850.038
303.15	0.7019	856.833
303.15	0.7938	864.539
303.15	0.8436	869.72
303.15	0.8941	876.764
303.15	0.9546	884.925
308.15	0.0595	817.544
308.15	0.1021	819.514
308.15	0.1430	821.37
308.15	0.2012	823.957
308.15	0.2633	826.723
308.15	0.3122	827.934
308.15	0.4113	832.902
308.15	0.4919	836.434
308.15	0.5973	841.825
308.15	0.7019	848.372
308.15	0.7938	855.829
308.15	0.8436	860.863
308.15	0.8941	867.723
308.15	0.9546	875.69
313.15	0.0595	813.972
313.15	0.1021	815.903
313.15	0.1430	817.713
313.15	0.2012	820.239
313.15	0.2633	822.931
313.15	0.3122	824.111
313.15	0.4113	828.963
313.15	0.4919	832.42
313.15	0.5973	837.701
313.15	0.7019	844.123
313.15	0.7938	851.455
313.15	0.8436	856.411
313.15	0.8941	863.18
313.15	0.9546	871.049

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	0.0595	1373.2
293.15	0.1021	1379.6
293.15	0.1430	1386.6
293.15	0.2012	1396.5
293.15	0.2633	1407.3
293.15	0.3122	1412.6
293.15	0.4113	1433.8
293.15	0.4919	1450.2
293.15	0.5973	1475.6
293.15	0.7019	1508.3
293.15	0.7938	1546.3
293.15	0.8436	1573.2
293.15	0.8941	1609.4
293.15	0.9546	1651.7
298.15	0.0595	1356.2
298.15	0.1021	1362.6
298.15	0.1430	1369.4
298.15	0.2012	1379.3
298.15	0.2633	1389.9
298.15	0.3122	1397.8
298.15	0.4113	1415.9
298.15	0.4919	1432.0
298.15	0.5973	1457.1
298.15	0.7019	1489.0
298.15	0.7938	1526.5
298.15	0.8436	1551.8
298.15	0.8941	1582.4
298.15	0.9546	1627.9
303.15	0.0595	1338.9
303.15	0.1021	1345.7
303.15	0.1430	1352.5
303.15	0.2012	1362.3
303.15	0.2633	1372.1
303.15	0.3122	1379.9
303.15	0.4113	1398.3
303.15	0.4919	1414.0
303.15	0.5973	1438.7
303.15	0.7019	1469.9
303.15	0.7938	1506.3
303.15	0.8436	1530.5
303.15	0.8941	1559.9
303.15	0.9546	1604.9
308.15	0.0595	1322.8
308.15	0.1021	1329.0
308.15	0.1430	1335.8
308.15	0.2012	1345.5
308.15	0.2633	1355.7
308.15	0.3122	1360.7
308.15	0.4113	1380.8
308.15	0.4919	1396.4
308.15	0.5973	1420.5
308.15	0.7019	1451.2
308.15	0.7938	1487.3
308.15	0.8436	1512.4
308.15	0.8941	1546.7
308.15	0.9546	1586.8
313.15	0.0595	1306.6
313.15	0.1021	1313.3
313.15	0.1430	1319.7
313.15	0.2012	1329.0
313.15	0.2633	1339.1
313.15	0.3122	1343.9
313.15	0.4113	1363.5
313.15	0.4919	1378.9
313.15	0.5973	1402.6
313.15	0.7019	1432.8
313.15	0.7938	1468.2
313.15	0.8436	1492.4
313.15	0.8941	1526.1
313.15	0.9546	1565.6

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	0.0595	1373.2
293.15	0.1021	1379.6
293.15	0.1430	1386.6
293.15	0.2012	1396.5
293.15	0.2633	1407.3
293.15	0.3122	1412.6
293.15	0.4113	1433.8
293.15	0.4919	1450.2
293.15	0.5973	1475.6
293.15	0.7019	1508.3
293.15	0.7938	1546.3
293.15	0.8436	1573.2
293.15	0.8941	1609.4
293.15	0.9546	1651.7
298.15	0.0595	1356.2
298.15	0.1021	1362.6
298.15	0.1430	1369.4
298.15	0.2012	1379.3
298.15	0.2633	1389.9
298.15	0.3122	1397.8
298.15	0.4113	1415.9
298.15	0.4919	1432.0
298.15	0.5973	1457.1
298.15	0.7019	1489.0
298.15	0.7938	1526.5
298.15	0.8436	1551.8
298.15	0.8941	1582.4
298.15	0.9546	1627.9
303.15	0.0595	1338.9
303.15	0.1021	1345.7
303.15	0.1430	1352.5
303.15	0.2012	1362.3
303.15	0.2633	1372.1
303.15	0.3122	1379.9
303.15	0.4113	1398.3
303.15	0.4919	1414.0
303.15	0.5973	1438.7
303.15	0.7019	1469.9
303.15	0.7938	1506.3
303.15	0.8436	1530.5
303.15	0.8941	1559.9
303.15	0.9546	1604.9
308.15	0.0595	1322.8
308.15	0.1021	1329.0
308.15	0.1430	1335.8
308.15	0.2012	1345.5
308.15	0.2633	1355.7
308.15	0.3122	1360.7
308.15	0.4113	1380.8
308.15	0.4919	1396.4
308.15	0.5973	1420.5
308.15	0.7019	1451.2
308.15	0.7938	1487.3
308.15	0.8436	1512.4
308.15	0.8941	1546.7
308.15	0.9546	1586.8
313.15	0.0595	1306.6
313.15	0.1021	1313.3
313.15	0.1430	1319.7
313.15	0.2012	1329.0
313.15	0.2633	1339.1
313.15	0.3122	1343.9
313.15	0.4113	1363.5
313.15	0.4919	1378.9
313.15	0.5973	1402.6
313.15	0.7019	1432.8
313.15	0.7938	1468.2
313.15	0.8436	1492.4
313.15	0.8941	1526.1
313.15	0.9546	1565.6

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
293.15	0.0595	-1.8380e-07
293.15	0.1021	-3.0090e-07
293.15	0.1430	-3.8960e-07
293.15	0.2012	-4.7630e-07
293.15	0.2633	-5.3080e-07
293.15	0.3122	-4.2300e-07
293.15	0.4113	-4.2300e-07
293.15	0.4919	-2.9750e-07
293.15	0.5973	-1.3590e-07
293.15	0.7019	1.2400e-08
293.15	0.7938	9.2800e-08
293.15	0.8436	1.0410e-07
293.15	0.8941	1.0250e-07
293.15	0.9546	2.6400e-08
298.15	0.0595	-1.8160e-07
298.15	0.1021	-2.9490e-07
298.15	0.1430	-3.7970e-07
298.15	0.2012	-4.6180e-07
298.15	0.2633	-5.1150e-07
298.15	0.3122	-4.2150e-07
298.15	0.4113	-4.0110e-07
298.15	0.4919	-2.7640e-07
298.15	0.5973	-1.1620e-07
298.15	0.7019	2.9700e-08
298.15	0.7938	1.0650e-07
298.15	0.8436	1.1500e-07
298.15	0.8941	1.0370e-07
298.15	0.9546	2.8900e-08
303.15	0.0595	-1.8070e-07
303.15	0.1021	-2.9050e-07
303.15	0.1430	-3.7140e-07
303.15	0.2012	-4.4870e-07
303.15	0.2633	-4.9490e-07
303.15	0.3122	-4.2080e-07
303.15	0.4113	-3.8090e-07
303.15	0.4919	-2.5630e-07
303.15	0.5973	-9.7400e-08
303.15	0.7019	4.6500e-08
303.15	0.7938	1.1970e-07
303.15	0.8436	1.2560e-07
303.15	0.8941	1.0450e-07
303.15	0.9546	3.1400e-08
308.15	0.0595	-1.7820e-07
308.15	0.1021	-2.8530e-07
308.15	0.1430	-3.6380e-07
308.15	0.2012	-4.3640e-07
308.15	0.2633	-4.7750e-07
308.15	0.3122	-4.2010e-07
308.15	0.4113	-3.6150e-07
308.15	0.4919	-2.3740e-07
308.15	0.5973	-7.9400e-08
308.15	0.7019	6.2200e-08
308.15	0.7938	1.3230e-07
308.15	0.8436	1.3560e-07
308.15	0.8941	1.0650e-07
308.15	0.9546	3.3700e-08
313.15	0.0595	-1.7950e-07
313.15	0.1021	-2.7430e-07
313.15	0.1430	-3.4980e-07
313.15	0.2012	-4.1960e-07
313.15	0.2633	-4.5670e-07
313.15	0.3122	-4.3040e-07
313.15	0.4113	-3.3810e-07
313.15	0.4919	-2.1480e-07
313.15	0.5973	-5.8500e-08
313.15	0.7019	8.0400e-08
313.15	0.7938	1.4680e-07
313.15	0.8436	1.4750e-07
313.15	0.8941	1.0740e-07
313.15	0.9546	3.6900e-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
293.15	0.0595	-1.8380e-07
293.15	0.1021	-3.0090e-07
293.15	0.1430	-3.8960e-07
293.15	0.2012	-4.7630e-07
293.15	0.2633	-5.3080e-07
293.15	0.3122	-4.2300e-07
293.15	0.4113	-4.2300e-07
293.15	0.4919	-2.9750e-07
293.15	0.5973	-1.3590e-07
293.15	0.7019	1.2400e-08
293.15	0.7938	9.2800e-08
293.15	0.8436	1.0410e-07
293.15	0.8941	1.0250e-07
293.15	0.9546	2.6400e-08
298.15	0.0595	-1.8160e-07
298.15	0.1021	-2.9490e-07
298.15	0.1430	-3.7970e-07
298.15	0.2012	-4.6180e-07
298.15	0.2633	-5.1150e-07
298.15	0.3122	-4.2150e-07
298.15	0.4113	-4.0110e-07
298.15	0.4919	-2.7640e-07
298.15	0.5973	-1.1620e-07
298.15	0.7019	2.9700e-08
298.15	0.7938	1.0650e-07
298.15	0.8436	1.1500e-07
298.15	0.8941	1.0370e-07
298.15	0.9546	2.8900e-08
303.15	0.0595	-1.8070e-07
303.15	0.1021	-2.9050e-07
303.15	0.1430	-3.7140e-07
303.15	0.2012	-4.4870e-07
303.15	0.2633	-4.9490e-07
303.15	0.3122	-4.2080e-07
303.15	0.4113	-3.8090e-07
303.15	0.4919	-2.5630e-07
303.15	0.5973	-9.7400e-08
303.15	0.7019	4.6500e-08
303.15	0.7938	1.1970e-07
303.15	0.8436	1.2560e-07
303.15	0.8941	1.0450e-07
303.15	0.9546	3.1400e-08
308.15	0.0595	-1.7820e-07
308.15	0.1021	-2.8530e-07
308.15	0.1430	-3.6380e-07
308.15	0.2012	-4.3640e-07
308.15	0.2633	-4.7750e-07
308.15	0.3122	-4.2010e-07
308.15	0.4113	-3.6150e-07
308.15	0.4919	-2.3740e-07
308.15	0.5973	-7.9400e-08
308.15	0.7019	6.2200e-08
308.15	0.7938	1.3230e-07
308.15	0.8436	1.3560e-07
308.15	0.8941	1.0650e-07
308.15	0.9546	3.3700e-08
313.15	0.0595	-1.7950e-07
313.15	0.1021	-2.7430e-07
313.15	0.1430	-3.4980e-07
313.15	0.2012	-4.1960e-07
313.15	0.2633	-4.5670e-07
313.15	0.3122	-4.3040e-07
313.15	0.4113	-3.3810e-07
313.15	0.4919	-2.1480e-07
313.15	0.5973	-5.8500e-08
313.15	0.7019	8.0400e-08
313.15	0.7938	1.4680e-07
313.15	0.8436	1.4750e-07
313.15	0.8941	1.0740e-07
313.15	0.9546	3.6900e-08

Sources

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