Mixture of 1-Decanol + 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	0.0424	0.0110
298.15	0.1063	0.0106
298.15	0.1512	0.0104
298.15	0.1995	0.0099
298.15	0.2511	0.0094
298.15	0.2957	0.0088
298.15	0.3961	0.0074
298.15	0.4929	0.0060
298.15	0.6090	0.0045
298.15	0.6962	0.0036
298.15	0.7975	0.0027
298.15	0.8550	0.0022
298.15	0.9054	0.0019
298.15	0.9591	0.0016
303.15	0.0424	0.0090
303.15	0.1063	0.0087
303.15	0.1512	0.0084
303.15	0.1995	0.0081
303.15	0.2511	0.0077
303.15	0.2957	0.0072
303.15	0.3961	0.0062
303.15	0.4929	0.0051
303.15	0.6090	0.0039
303.15	0.6962	0.0031
303.15	0.7975	0.0023
303.15	0.8550	0.0020
303.15	0.9054	0.0017
303.15	0.9591	0.0014
308.15	0.0424	0.0073
308.15	0.1063	0.0071
308.15	0.1512	0.0069
308.15	0.1995	0.0066
308.15	0.2511	0.0062
308.15	0.2957	0.0059
308.15	0.3961	0.0050
308.15	0.4929	0.0042
308.15	0.6090	0.0033
308.15	0.6962	0.0027
308.15	0.7975	0.0020
308.15	0.8550	0.0017
308.15	0.9054	0.0015
308.15	0.9591	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	0.0424	0.0110
298.15	0.1063	0.0106
298.15	0.1512	0.0104
298.15	0.1995	0.0099
298.15	0.2511	0.0094
298.15	0.2957	0.0088
298.15	0.3961	0.0074
298.15	0.4929	0.0060
298.15	0.6090	0.0045
298.15	0.6962	0.0036
298.15	0.7975	0.0027
298.15	0.8550	0.0022
298.15	0.9054	0.0019
298.15	0.9591	0.0016
303.15	0.0424	0.0090
303.15	0.1063	0.0087
303.15	0.1512	0.0084
303.15	0.1995	0.0081
303.15	0.2511	0.0077
303.15	0.2957	0.0072
303.15	0.3961	0.0062
303.15	0.4929	0.0051
303.15	0.6090	0.0039
303.15	0.6962	0.0031
303.15	0.7975	0.0023
303.15	0.8550	0.0020
303.15	0.9054	0.0017
303.15	0.9591	0.0014
308.15	0.0424	0.0073
308.15	0.1063	0.0071
308.15	0.1512	0.0069
308.15	0.1995	0.0066
308.15	0.2511	0.0062
308.15	0.2957	0.0059
308.15	0.3961	0.0050
308.15	0.4929	0.0042
308.15	0.6090	0.0033
308.15	0.6962	0.0027
308.15	0.7975	0.0020
308.15	0.8550	0.0017
308.15	0.9054	0.0015
308.15	0.9591	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	0.0424	831.534
293.15	0.1063	834.058
293.15	0.1512	835.766
293.15	0.1995	837.56
293.15	0.2511	839.445
293.15	0.2957	841.022
293.15	0.3961	844.521
293.15	0.4929	848.18
293.15	0.6090	853.458
293.15	0.6962	858.67
293.15	0.7975	866.833
293.15	0.8550	872.943
293.15	0.9054	879.622
293.15	0.9591	888.704
298.15	0.0424	828.092
298.15	0.1063	830.545
298.15	0.1512	832.202
298.15	0.1995	833.938
298.15	0.2511	835.76
298.15	0.2957	837.289
298.15	0.3961	840.693
298.15	0.4929	844.262
298.15	0.6090	849.415
298.15	0.6962	854.51
298.15	0.7975	862.525
298.15	0.8550	868.535
298.15	0.9054	875.128
298.15	0.9591	884.107
303.15	0.0424	824.641
303.15	0.1063	827.029
303.15	0.1512	828.635
303.15	0.1995	830.31
303.15	0.2511	832.075
303.15	0.2957	833.56
303.15	0.3961	836.868
303.15	0.4929	840.345
303.15	0.6090	845.37
303.15	0.6962	850.353
303.15	0.7975	858.212
303.15	0.8550	864.125
303.15	0.9054	870.631
303.15	0.9591	879.506
308.15	0.0424	821.178
308.15	0.1063	823.508
308.15	0.1512	825.064
308.15	0.1995	826.684
308.15	0.2511	828.392
308.15	0.2957	829.829
308.15	0.3961	833.045
308.15	0.4929	836.429
308.15	0.6090	841.323
308.15	0.6962	846.189
308.15	0.7975	853.898
308.15	0.8550	859.714
308.15	0.9054	866.124
308.15	0.9591	874.895
313.15	0.0424	817.698
313.15	0.1063	819.969
313.15	0.1512	821.476
313.15	0.1995	823.045
313.15	0.2511	824.7
313.15	0.2957	826.089
313.15	0.3961	829.21
313.15	0.4929	832.502
313.15	0.6090	837.271
313.15	0.6962	842.017
313.15	0.7975	849.57
313.15	0.8550	855.287
313.15	0.9054	861.605
313.15	0.9591	870.264

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	0.0424	831.534
293.15	0.1063	834.058
293.15	0.1512	835.766
293.15	0.1995	837.56
293.15	0.2511	839.445
293.15	0.2957	841.022
293.15	0.3961	844.521
293.15	0.4929	848.18
293.15	0.6090	853.458
293.15	0.6962	858.67
293.15	0.7975	866.833
293.15	0.8550	872.943
293.15	0.9054	879.622
293.15	0.9591	888.704
298.15	0.0424	828.092
298.15	0.1063	830.545
298.15	0.1512	832.202
298.15	0.1995	833.938
298.15	0.2511	835.76
298.15	0.2957	837.289
298.15	0.3961	840.693
298.15	0.4929	844.262
298.15	0.6090	849.415
298.15	0.6962	854.51
298.15	0.7975	862.525
298.15	0.8550	868.535
298.15	0.9054	875.128
298.15	0.9591	884.107
303.15	0.0424	824.641
303.15	0.1063	827.029
303.15	0.1512	828.635
303.15	0.1995	830.31
303.15	0.2511	832.075
303.15	0.2957	833.56
303.15	0.3961	836.868
303.15	0.4929	840.345
303.15	0.6090	845.37
303.15	0.6962	850.353
303.15	0.7975	858.212
303.15	0.8550	864.125
303.15	0.9054	870.631
303.15	0.9591	879.506
308.15	0.0424	821.178
308.15	0.1063	823.508
308.15	0.1512	825.064
308.15	0.1995	826.684
308.15	0.2511	828.392
308.15	0.2957	829.829
308.15	0.3961	833.045
308.15	0.4929	836.429
308.15	0.6090	841.323
308.15	0.6962	846.189
308.15	0.7975	853.898
308.15	0.8550	859.714
308.15	0.9054	866.124
308.15	0.9591	874.895
313.15	0.0424	817.698
313.15	0.1063	819.969
313.15	0.1512	821.476
313.15	0.1995	823.045
313.15	0.2511	824.7
313.15	0.2957	826.089
313.15	0.3961	829.21
313.15	0.4929	832.502
313.15	0.6090	837.271
313.15	0.6962	842.017
313.15	0.7975	849.57
313.15	0.8550	855.287
313.15	0.9054	861.605
313.15	0.9591	870.264

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	0.0424	1402.1
293.15	0.1063	1408.9
293.15	0.1512	1414.8
293.15	0.1995	1420.8
293.15	0.2511	1427.1
293.15	0.2957	1432.6
293.15	0.3961	1445.5
293.15	0.4929	1459.7
293.15	0.6090	1481.8
293.15	0.6962	1504.6
293.15	0.7975	1541.1
293.15	0.8550	1570.1
293.15	0.9054	1602.3
293.15	0.9591	1648.1
298.15	0.0424	1384.9
298.15	0.1063	1391.6
298.15	0.1512	1397.5
298.15	0.1995	1403.3
298.15	0.2511	1409.5
298.15	0.2957	1414.9
298.15	0.3961	1427.6
298.15	0.4929	1441.5
298.15	0.6090	1463.1
298.15	0.6962	1485.4
298.15	0.7975	1521.3
298.15	0.8550	1549.7
298.15	0.9054	1581.4
298.15	0.9591	1626.4
303.15	0.0424	1367.8
303.15	0.1063	1374.7
303.15	0.1512	1380.3
303.15	0.1995	1386.1
303.15	0.2511	1392.1
303.15	0.2957	1397.5
303.15	0.3961	1409.8
303.15	0.4929	1423.5
303.15	0.6090	1444.5
303.15	0.6962	1466.5
303.15	0.7975	1501.6
303.15	0.8550	1529.5
303.15	0.9054	1560.8
303.15	0.9591	1604.9
308.15	0.0424	1350.9
308.15	0.1063	1358.0
308.15	0.1512	1363.4
308.15	0.1995	1369.1
308.15	0.2511	1375.0
308.15	0.2957	1380.3
308.15	0.3961	1392.3
308.15	0.4929	1405.6
308.15	0.6090	1426.1
308.15	0.6962	1447.5
308.15	0.7975	1481.9
308.15	0.8550	1509.4
308.15	0.9054	1540.1
308.15	0.9591	1583.6
313.15	0.0424	1334.2
313.15	0.1063	1341.6
313.15	0.1512	1346.8
313.15	0.1995	1352.3
313.15	0.2511	1358.1
313.15	0.2957	1363.2
313.15	0.3961	1375.0
313.15	0.4929	1387.9
313.15	0.6090	1407.9
313.15	0.6962	1428.6
313.15	0.7975	1462.5
313.15	0.8550	1489.4
313.15	0.9054	1519.8
313.15	0.9591	1562.4

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	0.0424	1402.1
293.15	0.1063	1408.9
293.15	0.1512	1414.8
293.15	0.1995	1420.8
293.15	0.2511	1427.1
293.15	0.2957	1432.6
293.15	0.3961	1445.5
293.15	0.4929	1459.7
293.15	0.6090	1481.8
293.15	0.6962	1504.6
293.15	0.7975	1541.1
293.15	0.8550	1570.1
293.15	0.9054	1602.3
293.15	0.9591	1648.1
298.15	0.0424	1384.9
298.15	0.1063	1391.6
298.15	0.1512	1397.5
298.15	0.1995	1403.3
298.15	0.2511	1409.5
298.15	0.2957	1414.9
298.15	0.3961	1427.6
298.15	0.4929	1441.5
298.15	0.6090	1463.1
298.15	0.6962	1485.4
298.15	0.7975	1521.3
298.15	0.8550	1549.7
298.15	0.9054	1581.4
298.15	0.9591	1626.4
303.15	0.0424	1367.8
303.15	0.1063	1374.7
303.15	0.1512	1380.3
303.15	0.1995	1386.1
303.15	0.2511	1392.1
303.15	0.2957	1397.5
303.15	0.3961	1409.8
303.15	0.4929	1423.5
303.15	0.6090	1444.5
303.15	0.6962	1466.5
303.15	0.7975	1501.6
303.15	0.8550	1529.5
303.15	0.9054	1560.8
303.15	0.9591	1604.9
308.15	0.0424	1350.9
308.15	0.1063	1358.0
308.15	0.1512	1363.4
308.15	0.1995	1369.1
308.15	0.2511	1375.0
308.15	0.2957	1380.3
308.15	0.3961	1392.3
308.15	0.4929	1405.6
308.15	0.6090	1426.1
308.15	0.6962	1447.5
308.15	0.7975	1481.9
308.15	0.8550	1509.4
308.15	0.9054	1540.1
308.15	0.9591	1583.6
313.15	0.0424	1334.2
313.15	0.1063	1341.6
313.15	0.1512	1346.8
313.15	0.1995	1352.3
313.15	0.2511	1358.1
313.15	0.2957	1363.2
313.15	0.3961	1375.0
313.15	0.4929	1387.9
313.15	0.6090	1407.9
313.15	0.6962	1428.6
313.15	0.7975	1462.5
313.15	0.8550	1489.4
313.15	0.9054	1519.8
313.15	0.9591	1562.4

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	0.0424	-1.3860e-07
293.15	0.1063	-3.1500e-07
293.15	0.1512	-3.9620e-07
293.15	0.1995	-4.4940e-07
293.15	0.2511	-4.7170e-07
293.15	0.2957	-4.5840e-07
293.15	0.3961	-3.4450e-07
293.15	0.4929	-1.8210e-07
293.15	0.6090	2.5900e-08
293.15	0.6962	1.4440e-07
293.15	0.7975	2.1870e-07
293.15	0.8550	2.2040e-07
293.15	0.9054	1.8440e-07
293.15	0.9591	9.0200e-08
298.15	0.0424	-1.3750e-07
298.15	0.1063	-3.0670e-07
298.15	0.1512	-3.8320e-07
298.15	0.1995	-4.3120e-07
298.15	0.2511	-4.4840e-07
298.15	0.2957	-4.3240e-07
298.15	0.3961	-3.1630e-07
298.15	0.4929	-1.5440e-07
298.15	0.6090	5.2200e-08
298.15	0.6962	1.6920e-07
298.15	0.7975	2.3850e-07
298.15	0.8550	2.3650e-07
298.15	0.9054	1.9530e-07
298.15	0.9591	9.4400e-08
303.15	0.0424	-1.3590e-07
303.15	0.1063	-2.9920e-07
303.15	0.1512	-3.7080e-07
303.15	0.1995	-4.1290e-07
303.15	0.2511	-4.2620e-07
303.15	0.2957	-4.0810e-07
303.15	0.3961	-2.8960e-07
303.15	0.4929	-1.2760e-07
303.15	0.6090	7.7900e-08
303.15	0.6962	1.9270e-07
303.15	0.7975	2.5790e-07
303.15	0.8550	2.5190e-07
303.15	0.9054	2.0560e-07
303.15	0.9591	9.8000e-08
308.15	0.0424	-1.3580e-07
308.15	0.1063	-2.9450e-07
308.15	0.1512	-3.6140e-07
308.15	0.1995	-3.9850e-07
308.15	0.2511	-4.0750e-07
308.15	0.2957	-3.8650e-07
308.15	0.3961	-2.6580e-07
308.15	0.4929	-1.0330e-07
308.15	0.6090	1.0190e-07
308.15	0.6962	2.1550e-07
308.15	0.7975	2.7620e-07
308.15	0.8550	2.6620e-07
308.15	0.9054	2.1560e-07
308.15	0.9591	1.0140e-07
313.15	0.0424	-1.5120e-07
313.15	0.1063	-3.0390e-07
313.15	0.1512	-3.6540e-07
313.15	0.1995	-3.9760e-07
313.15	0.2511	-4.0210e-07
313.15	0.2957	-3.7730e-07
313.15	0.3961	-2.5210e-07
313.15	0.4929	-8.7600e-08
313.15	0.6090	1.1870e-07
313.15	0.6962	2.3300e-07
313.15	0.7975	2.9150e-07
313.15	0.8550	2.7870e-07
313.15	0.9054	2.2430e-07
313.15	0.9591	1.0490e-07

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	0.0424	-1.3860e-07
293.15	0.1063	-3.1500e-07
293.15	0.1512	-3.9620e-07
293.15	0.1995	-4.4940e-07
293.15	0.2511	-4.7170e-07
293.15	0.2957	-4.5840e-07
293.15	0.3961	-3.4450e-07
293.15	0.4929	-1.8210e-07
293.15	0.6090	2.5900e-08
293.15	0.6962	1.4440e-07
293.15	0.7975	2.1870e-07
293.15	0.8550	2.2040e-07
293.15	0.9054	1.8440e-07
293.15	0.9591	9.0200e-08
298.15	0.0424	-1.3750e-07
298.15	0.1063	-3.0670e-07
298.15	0.1512	-3.8320e-07
298.15	0.1995	-4.3120e-07
298.15	0.2511	-4.4840e-07
298.15	0.2957	-4.3240e-07
298.15	0.3961	-3.1630e-07
298.15	0.4929	-1.5440e-07
298.15	0.6090	5.2200e-08
298.15	0.6962	1.6920e-07
298.15	0.7975	2.3850e-07
298.15	0.8550	2.3650e-07
298.15	0.9054	1.9530e-07
298.15	0.9591	9.4400e-08
303.15	0.0424	-1.3590e-07
303.15	0.1063	-2.9920e-07
303.15	0.1512	-3.7080e-07
303.15	0.1995	-4.1290e-07
303.15	0.2511	-4.2620e-07
303.15	0.2957	-4.0810e-07
303.15	0.3961	-2.8960e-07
303.15	0.4929	-1.2760e-07
303.15	0.6090	7.7900e-08
303.15	0.6962	1.9270e-07
303.15	0.7975	2.5790e-07
303.15	0.8550	2.5190e-07
303.15	0.9054	2.0560e-07
303.15	0.9591	9.8000e-08
308.15	0.0424	-1.3580e-07
308.15	0.1063	-2.9450e-07
308.15	0.1512	-3.6140e-07
308.15	0.1995	-3.9850e-07
308.15	0.2511	-4.0750e-07
308.15	0.2957	-3.8650e-07
308.15	0.3961	-2.6580e-07
308.15	0.4929	-1.0330e-07
308.15	0.6090	1.0190e-07
308.15	0.6962	2.1550e-07
308.15	0.7975	2.7620e-07
308.15	0.8550	2.6620e-07
308.15	0.9054	2.1560e-07
308.15	0.9591	1.0140e-07
313.15	0.0424	-1.5120e-07
313.15	0.1063	-3.0390e-07
313.15	0.1512	-3.6540e-07
313.15	0.1995	-3.9760e-07
313.15	0.2511	-4.0210e-07
313.15	0.2957	-3.7730e-07
313.15	0.3961	-2.5210e-07
313.15	0.4929	-8.7600e-08
313.15	0.6090	1.1870e-07
313.15	0.6962	2.3300e-07
313.15	0.7975	2.9150e-07
313.15	0.8550	2.7870e-07
313.15	0.9054	2.2430e-07
313.15	0.9591	1.0490e-07

Sources

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