Mixture of Isopropyl Alcohol + Ethylenediamine

Datasets

1. η - Viscosity, Pa*s (2)
2. Excess molar enthalpy (molar enthalpy (2)
3. ρ_l - Mass density, kg/m3 (2)
4. c_sound,fluid - Speed of Sound, m/s (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	0.0557	0.0020
298.15	0.1036	0.0020
298.15	0.1560	0.0020
298.15	0.2011	0.0020
298.15	0.2548	0.0020
298.15	0.3018	0.0019
298.15	0.3892	0.0019
298.15	0.5109	0.0018
298.15	0.6050	0.0017
298.15	0.6988	0.0016
298.15	0.7969	0.0015
298.15	0.8369	0.0015
298.15	0.8931	0.0015
298.15	0.9409	0.0014
303.15	0.0557	0.0018
303.15	0.1036	0.0017
303.15	0.1560	0.0017
303.15	0.2011	0.0017
303.15	0.2548	0.0017
303.15	0.3018	0.0017
303.15	0.3892	0.0016
303.15	0.5109	0.0016
303.15	0.6050	0.0015
303.15	0.6988	0.0014
303.15	0.7969	0.0014
303.15	0.8369	0.0013
303.15	0.8931	0.0013
303.15	0.9409	0.0013
308.15	0.0557	0.0016
308.15	0.1036	0.0015
308.15	0.1560	0.0015
308.15	0.2011	0.0015
308.15	0.2548	0.0015
308.15	0.3018	0.0015
308.15	0.3892	0.0014
308.15	0.5109	0.0014
308.15	0.6050	0.0013
308.15	0.6988	0.0013
308.15	0.7969	0.0012
308.15	0.8369	0.0012
308.15	0.8931	0.0012
308.15	0.9409	0.0011

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	0.0557	0.0020
298.15	0.1036	0.0020
298.15	0.1560	0.0020
298.15	0.2011	0.0020
298.15	0.2548	0.0020
298.15	0.3018	0.0019
298.15	0.3892	0.0019
298.15	0.5109	0.0018
298.15	0.6050	0.0017
298.15	0.6988	0.0016
298.15	0.7969	0.0015
298.15	0.8369	0.0015
298.15	0.8931	0.0015
298.15	0.9409	0.0014
303.15	0.0557	0.0018
303.15	0.1036	0.0017
303.15	0.1560	0.0017
303.15	0.2011	0.0017
303.15	0.2548	0.0017
303.15	0.3018	0.0017
303.15	0.3892	0.0016
303.15	0.5109	0.0016
303.15	0.6050	0.0015
303.15	0.6988	0.0014
303.15	0.7969	0.0014
303.15	0.8369	0.0013
303.15	0.8931	0.0013
303.15	0.9409	0.0013
308.15	0.0557	0.0016
308.15	0.1036	0.0015
308.15	0.1560	0.0015
308.15	0.2011	0.0015
308.15	0.2548	0.0015
308.15	0.3018	0.0015
308.15	0.3892	0.0014
308.15	0.5109	0.0014
308.15	0.6050	0.0013
308.15	0.6988	0.0013
308.15	0.7969	0.0012
308.15	0.8369	0.0012
308.15	0.8931	0.0012
308.15	0.9409	0.0011

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298 (Liquid)
• Pressure, kPa = 81.5 (Liquid)

Mole fraction of Ethylenediamine (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1001	-0.8760
0.2000	-1.5584
0.3007	-1.9323
0.4033	-1.9985
0.5073	-1.8215
0.5963	-1.5191
0.6988	-1.1516
0.7998	-0.7475
0.8998	-0.3533

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298 (Liquid)
• Pressure, kPa = 81.5 (Liquid)

Mole fraction of Ethylenediamine (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1001	-0.8760
0.2000	-1.5584
0.3007	-1.9323
0.4033	-1.9985
0.5073	-1.8215
0.5963	-1.5191
0.6988	-1.1516
0.7998	-0.7475
0.8998	-0.3533

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Ethylenediamine (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0557	293.15	793.696
0.0557	298.15	789.425
0.0557	303.15	785.1
0.0557	308.15	780.72
0.0557	313.15	776.266
0.1036	293.15	800.705
0.1036	298.15	796.388
0.1036	303.15	792.016
0.1036	308.15	787.599
0.1036	313.15	783.114
0.1560	293.15	807.902
0.1560	298.15	803.523
0.1560	303.15	799.108
0.1560	308.15	794.649
0.1560	313.15	790.129
0.2011	293.15	813.922
0.2011	298.15	809.506
0.2011	303.15	805.044
0.2011	308.15	800.552
0.2011	313.15	796.005
0.2548	293.15	820.862
0.2548	298.15	816.397
0.2548	303.15	811.904
0.2548	308.15	807.374
0.2548	313.15	802.798
0.3018	293.15	826.514
0.3018	298.15	822.019
0.3018	303.15	817.496
0.3018	308.15	812.943
0.3018	313.15	808.346
0.3892	293.15	836.546
0.3892	298.15	832.023
0.3892	303.15	827.475
0.3892	308.15	822.898
0.3892	313.15	818.281
0.5109	293.15	849.474
0.5109	298.15	844.925
0.5109	303.15	840.354
0.5109	308.15	835.76
0.5109	313.15	831.131
0.6050	293.15	858.745
0.6050	298.15	854.173
0.6050	303.15	849.588
0.6050	308.15	844.983
0.6050	313.15	840.349
0.6988	293.15	868.4
0.6988	298.15	863.796
0.6988	303.15	859.186
0.6988	308.15	854.563
0.6988	313.15	849.909
0.7969	293.15	878.278
0.7969	298.15	873.662
0.7969	303.15	869.028
0.7969	308.15	864.38
0.7969	313.15	859.706
0.8369	293.15	881.835
0.8369	298.15	877.194
0.8369	303.15	872.546
0.8369	308.15	867.885
0.8369	313.15	863.196
0.8931	293.15	887.269
0.8931	298.15	882.613
0.8931	303.15	877.945
0.8931	308.15	873.264
0.8931	313.15	868.56
0.9409	293.15	892.34
0.9409	298.15	887.669
0.9409	303.15	882.985
0.9409	308.15	878.288
0.9409	313.15	873.569

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Ethylenediamine (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0557	293.15	793.696
0.0557	298.15	789.425
0.0557	303.15	785.1
0.0557	308.15	780.72
0.0557	313.15	776.266
0.1036	293.15	800.705
0.1036	298.15	796.388
0.1036	303.15	792.016
0.1036	308.15	787.599
0.1036	313.15	783.114
0.1560	293.15	807.902
0.1560	298.15	803.523
0.1560	303.15	799.108
0.1560	308.15	794.649
0.1560	313.15	790.129
0.2011	293.15	813.922
0.2011	298.15	809.506
0.2011	303.15	805.044
0.2011	308.15	800.552
0.2011	313.15	796.005
0.2548	293.15	820.862
0.2548	298.15	816.397
0.2548	303.15	811.904
0.2548	308.15	807.374
0.2548	313.15	802.798
0.3018	293.15	826.514
0.3018	298.15	822.019
0.3018	303.15	817.496
0.3018	308.15	812.943
0.3018	313.15	808.346
0.3892	293.15	836.546
0.3892	298.15	832.023
0.3892	303.15	827.475
0.3892	308.15	822.898
0.3892	313.15	818.281
0.5109	293.15	849.474
0.5109	298.15	844.925
0.5109	303.15	840.354
0.5109	308.15	835.76
0.5109	313.15	831.131
0.6050	293.15	858.745
0.6050	298.15	854.173
0.6050	303.15	849.588
0.6050	308.15	844.983
0.6050	313.15	840.349
0.6988	293.15	868.4
0.6988	298.15	863.796
0.6988	303.15	859.186
0.6988	308.15	854.563
0.6988	313.15	849.909
0.7969	293.15	878.278
0.7969	298.15	873.662
0.7969	303.15	869.028
0.7969	308.15	864.38
0.7969	313.15	859.706
0.8369	293.15	881.835
0.8369	298.15	877.194
0.8369	303.15	872.546
0.8369	308.15	867.885
0.8369	313.15	863.196
0.8931	293.15	887.269
0.8931	298.15	882.613
0.8931	303.15	877.945
0.8931	308.15	873.264
0.8931	313.15	868.56
0.9409	293.15	892.34
0.9409	298.15	887.669
0.9409	303.15	882.985
0.9409	308.15	878.288
0.9409	313.15	873.569

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Ethylenediamine (2) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0557	293.15	1187.2
0.0557	298.15	1169.4
0.0557	303.15	1151.7
0.0557	308.15	1134.0
0.0557	313.15	1116.4
0.1036	293.15	1213.8
0.1036	298.15	1195.9
0.1036	303.15	1178.0
0.1036	308.15	1160.1
0.1036	313.15	1142.2
0.1560	293.15	1241.5
0.1560	298.15	1223.4
0.1560	303.15	1205.3
0.1560	308.15	1187.3
0.1560	313.15	1169.4
0.2011	293.15	1265.8
0.2011	298.15	1247.6
0.2011	303.15	1229.4
0.2011	308.15	1211.2
0.2011	313.15	1193.2
0.2548	293.15	1295.1
0.2548	298.15	1276.6
0.2548	303.15	1258.2
0.2548	308.15	1239.8
0.2548	313.15	1221.6
0.3018	293.15	1320.2
0.3018	298.15	1301.6
0.3018	303.15	1283.0
0.3018	308.15	1264.5
0.3018	313.15	1246.1
0.3892	293.15	1366.4
0.3892	298.15	1347.5
0.3892	303.15	1328.5
0.3892	308.15	1309.7
0.3892	313.15	1291.2
0.5109	293.15	1430.5
0.5109	298.15	1410.9
0.5109	303.15	1391.5
0.5109	308.15	1372.1
0.5109	313.15	1353.4
0.6050	293.15	1478.9
0.6050	298.15	1458.9
0.6050	303.15	1439.0
0.6050	308.15	1419.1
0.6050	313.15	1399.4
0.6988	293.15	1530.6
0.6988	298.15	1510.0
0.6988	303.15	1489.5
0.6988	308.15	1469.1
0.6988	313.15	1449.1
0.7969	293.15	1584.3
0.7969	298.15	1563.2
0.7969	303.15	1542.1
0.7969	308.15	1521.1
0.7969	313.15	1500.5
0.8369	293.15	1605.3
0.8369	298.15	1583.7
0.8369	303.15	1562.4
0.8369	308.15	1541.2
0.8369	313.15	1520.3
0.8931	293.15	1635.6
0.8931	298.15	1613.9
0.8931	303.15	1592.1
0.8931	308.15	1570.6
0.8931	313.15	1549.4
0.9409	293.15	1662.9
0.9409	298.15	1640.7
0.9409	303.15	1618.7
0.9409	308.15	1596.8
0.9409	313.15	1575.4

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Ethylenediamine (2) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0557	293.15	1187.2
0.0557	298.15	1169.4
0.0557	303.15	1151.7
0.0557	308.15	1134.0
0.0557	313.15	1116.4
0.1036	293.15	1213.8
0.1036	298.15	1195.9
0.1036	303.15	1178.0
0.1036	308.15	1160.1
0.1036	313.15	1142.2
0.1560	293.15	1241.5
0.1560	298.15	1223.4
0.1560	303.15	1205.3
0.1560	308.15	1187.3
0.1560	313.15	1169.4
0.2011	293.15	1265.8
0.2011	298.15	1247.6
0.2011	303.15	1229.4
0.2011	308.15	1211.2
0.2011	313.15	1193.2
0.2548	293.15	1295.1
0.2548	298.15	1276.6
0.2548	303.15	1258.2
0.2548	308.15	1239.8
0.2548	313.15	1221.6
0.3018	293.15	1320.2
0.3018	298.15	1301.6
0.3018	303.15	1283.0
0.3018	308.15	1264.5
0.3018	313.15	1246.1
0.3892	293.15	1366.4
0.3892	298.15	1347.5
0.3892	303.15	1328.5
0.3892	308.15	1309.7
0.3892	313.15	1291.2
0.5109	293.15	1430.5
0.5109	298.15	1410.9
0.5109	303.15	1391.5
0.5109	308.15	1372.1
0.5109	313.15	1353.4
0.6050	293.15	1478.9
0.6050	298.15	1458.9
0.6050	303.15	1439.0
0.6050	308.15	1419.1
0.6050	313.15	1399.4
0.6988	293.15	1530.6
0.6988	298.15	1510.0
0.6988	303.15	1489.5
0.6988	308.15	1469.1
0.6988	313.15	1449.1
0.7969	293.15	1584.3
0.7969	298.15	1563.2
0.7969	303.15	1542.1
0.7969	308.15	1521.1
0.7969	313.15	1500.5
0.8369	293.15	1605.3
0.8369	298.15	1583.7
0.8369	303.15	1562.4
0.8369	308.15	1541.2
0.8369	313.15	1520.3
0.8931	293.15	1635.6
0.8931	298.15	1613.9
0.8931	303.15	1592.1
0.8931	308.15	1570.6
0.8931	313.15	1549.4
0.9409	293.15	1662.9
0.9409	298.15	1640.7
0.9409	303.15	1618.7
0.9409	308.15	1596.8
0.9409	313.15	1575.4

Sources

• Excess molar enthalpies of ethane-1,2-diamine plus primary and secondary alkanols (C1-C4) and correlation with Redlich-Kister, Wilson, NRTL and UNIQUAC models at T = 298 K
• Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Ethylenediamine with Alcohols at T = (293.15 to 313.15) K