Mixture of 1-Butanol + 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	0.0528	0.0026
298.15	0.1135	0.0026
298.15	0.1488	0.0026
298.15	0.2140	0.0025
298.15	0.2602	0.0025
298.15	0.3283	0.0024
298.15	0.3985	0.0023
298.15	0.5036	0.0022
298.15	0.5965	0.0020
298.15	0.7081	0.0018
298.15	0.7931	0.0017
298.15	0.8504	0.0016
298.15	0.8979	0.0015
298.15	0.9360	0.0015
303.15	0.0528	0.0023
303.15	0.1135	0.0023
303.15	0.1488	0.0023
303.15	0.2140	0.0022
303.15	0.2602	0.0022
303.15	0.3283	0.0021
303.15	0.3985	0.0021
303.15	0.5036	0.0019
303.15	0.5965	0.0018
303.15	0.7081	0.0016
303.15	0.7931	0.0015
303.15	0.8504	0.0014
303.15	0.8979	0.0014
303.15	0.9360	0.0013
308.15	0.0528	0.0020
308.15	0.1135	0.0020
308.15	0.1488	0.0020
308.15	0.2140	0.0020
308.15	0.2602	0.0019
308.15	0.3283	0.0019
308.15	0.3985	0.0018
308.15	0.5036	0.0017
308.15	0.5965	0.0016
308.15	0.7081	0.0015
308.15	0.7931	0.0014
308.15	0.8504	0.0013
308.15	0.8979	0.0013
308.15	0.9360	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	0.0528	0.0026
298.15	0.1135	0.0026
298.15	0.1488	0.0026
298.15	0.2140	0.0025
298.15	0.2602	0.0025
298.15	0.3283	0.0024
298.15	0.3985	0.0023
298.15	0.5036	0.0022
298.15	0.5965	0.0020
298.15	0.7081	0.0018
298.15	0.7931	0.0017
298.15	0.8504	0.0016
298.15	0.8979	0.0015
298.15	0.9360	0.0015
303.15	0.0528	0.0023
303.15	0.1135	0.0023
303.15	0.1488	0.0023
303.15	0.2140	0.0022
303.15	0.2602	0.0022
303.15	0.3283	0.0021
303.15	0.3985	0.0021
303.15	0.5036	0.0019
303.15	0.5965	0.0018
303.15	0.7081	0.0016
303.15	0.7931	0.0015
303.15	0.8504	0.0014
303.15	0.8979	0.0014
303.15	0.9360	0.0013
308.15	0.0528	0.0020
308.15	0.1135	0.0020
308.15	0.1488	0.0020
308.15	0.2140	0.0020
308.15	0.2602	0.0019
308.15	0.3283	0.0019
308.15	0.3985	0.0018
308.15	0.5036	0.0017
308.15	0.5965	0.0016
308.15	0.7081	0.0015
308.15	0.7931	0.0014
308.15	0.8504	0.0013
308.15	0.8979	0.0013
308.15	0.9360	0.0012

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
0.1003	-1.1504
0.2002	-2.035
0.3011	-2.4862
0.4024	-2.5117
0.5053	-2.2382
0.6097	-1.7928
0.6983	-1.3062
0.8000	-0.8037
0.8999	-0.3567

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
0.1003	-1.1504
0.2002	-2.035
0.3011	-2.4862
0.4024	-2.5117
0.5053	-2.2382
0.6097	-1.7928
0.6983	-1.3062
0.8000	-0.8037
0.8999	-0.3567

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
0.0528	293.15	815.585
0.0528	298.15	811.698
0.0528	303.15	807.785
0.0528	308.15	803.849
0.0528	313.15	799.876
0.1135	293.15	822.116
0.1135	298.15	818.144
0.1135	303.15	814.153
0.1135	308.15	810.137
0.1135	313.15	806.088
0.1488	293.15	825.769
0.1488	298.15	821.746
0.1488	303.15	817.703
0.1488	308.15	813.64
0.1488	313.15	809.548
0.2140	293.15	832.273
0.2140	298.15	828.164
0.2140	303.15	824.038
0.2140	308.15	819.892
0.2140	313.15	815.723
0.2602	293.15	836.674
0.2602	298.15	832.509
0.2602	303.15	828.329
0.2602	308.15	824.133
0.2602	313.15	819.91
0.3286	293.15	842.718
0.3286	298.15	838.245
0.3286	303.15	833.896
0.3286	308.15	829.828
0.3286	313.15	825.879
0.3985	293.15	848.216
0.3985	298.15	843.943
0.3985	303.15	839.656
0.3985	308.15	835.352
0.3985	313.15	831.025
0.5036	293.15	856.28
0.5036	298.15	851.943
0.5036	303.15	847.599
0.5036	308.15	843.235
0.5036	313.15	838.849
0.5965	293.15	863.365
0.5965	298.15	858.974
0.5965	303.15	854.57
0.5965	308.15	850.157
0.5965	313.15	845.718
0.7081	293.15	872.153
0.7081	298.15	867.696
0.7081	303.15	863.224
0.7081	308.15	858.739
0.7081	313.15	854.232
0.7931	293.15	879.359
0.7931	298.15	874.839
0.7931	303.15	870.306
0.7931	308.15	865.762
0.7931	313.15	861.194
0.8504	293.15	884.315
0.8504	298.15	879.75
0.8504	303.15	875.173
0.8504	308.15	870.584
0.8504	313.15	865.971
0.8979	293.15	888.772
0.8979	298.15	884.168
0.8979	303.15	879.552
0.8979	308.15	874.924
0.8979	313.15	870.277
0.9360	293.15	892.567
0.9360	298.15	887.932
0.9360	303.15	883.288
0.9360	308.15	878.628
0.9360	313.15	873.95

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
0.0528	293.15	815.585
0.0528	298.15	811.698
0.0528	303.15	807.785
0.0528	308.15	803.849
0.0528	313.15	799.876
0.1135	293.15	822.116
0.1135	298.15	818.144
0.1135	303.15	814.153
0.1135	308.15	810.137
0.1135	313.15	806.088
0.1488	293.15	825.769
0.1488	298.15	821.746
0.1488	303.15	817.703
0.1488	308.15	813.64
0.1488	313.15	809.548
0.2140	293.15	832.273
0.2140	298.15	828.164
0.2140	303.15	824.038
0.2140	308.15	819.892
0.2140	313.15	815.723
0.2602	293.15	836.674
0.2602	298.15	832.509
0.2602	303.15	828.329
0.2602	308.15	824.133
0.2602	313.15	819.91
0.3286	293.15	842.718
0.3286	298.15	838.245
0.3286	303.15	833.896
0.3286	308.15	829.828
0.3286	313.15	825.879
0.3985	293.15	848.216
0.3985	298.15	843.943
0.3985	303.15	839.656
0.3985	308.15	835.352
0.3985	313.15	831.025
0.5036	293.15	856.28
0.5036	298.15	851.943
0.5036	303.15	847.599
0.5036	308.15	843.235
0.5036	313.15	838.849
0.5965	293.15	863.365
0.5965	298.15	858.974
0.5965	303.15	854.57
0.5965	308.15	850.157
0.5965	313.15	845.718
0.7081	293.15	872.153
0.7081	298.15	867.696
0.7081	303.15	863.224
0.7081	308.15	858.739
0.7081	313.15	854.232
0.7931	293.15	879.359
0.7931	298.15	874.839
0.7931	303.15	870.306
0.7931	308.15	865.762
0.7931	313.15	861.194
0.8504	293.15	884.315
0.8504	298.15	879.75
0.8504	303.15	875.173
0.8504	308.15	870.584
0.8504	313.15	865.971
0.8979	293.15	888.772
0.8979	298.15	884.168
0.8979	303.15	879.552
0.8979	308.15	874.924
0.8979	313.15	870.277
0.9360	293.15	892.567
0.9360	298.15	887.932
0.9360	303.15	883.288
0.9360	308.15	878.628
0.9360	313.15	873.95

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
0.0528	293.15	1279.7
0.0528	298.15	1262.9
0.0528	303.15	1245.9
0.0528	308.15	1228.5
0.0528	313.15	1210.7
0.1135	293.15	1302.1
0.1135	298.15	1285.0
0.1135	303.15	1267.9
0.1135	308.15	1250.7
0.1135	313.15	1233.6
0.1488	293.15	1315.9
0.1488	298.15	1298.6
0.1488	303.15	1281.4
0.1488	308.15	1264.3
0.1488	313.15	1247.2
0.2140	293.15	1341.7
0.2140	298.15	1324.3
0.2140	303.15	1306.8
0.2140	308.15	1289.5
0.2140	313.15	1272.3
0.2602	293.15	1360.5
0.2602	298.15	1342.9
0.2602	303.15	1325.3
0.2602	308.15	1307.8
0.2602	313.15	1290.4
0.3286	293.15	1387.1
0.3286	298.15	1368.8
0.3286	303.15	1350.9
0.3286	308.15	1333.6
0.3286	313.15	1315.8
0.3985	293.15	1414.5
0.3985	298.15	1396.3
0.3985	303.15	1378.1
0.3985	308.15	1360.0
0.3985	313.15	1341.9
0.5036	293.15	1456.5
0.5036	298.15	1437.7
0.5036	303.15	1419.1
0.5036	308.15	1400.4
0.5036	313.15	1381.7
0.5965	293.15	1494.7
0.5965	298.15	1475.5
0.5965	303.15	1456.3
0.5965	308.15	1437.1
0.5965	313.15	1418.1
0.7081	293.15	1543.9
0.7081	298.15	1523.9
0.7081	303.15	1504.0
0.7081	308.15	1484.2
0.7081	313.15	1464.4
0.7931	293.15	1584.7
0.7931	298.15	1564.1
0.7931	303.15	1543.5
0.7931	308.15	1523.0
0.7931	313.15	1502.7
0.8504	293.15	1613.6
0.8504	298.15	1592.5
0.8504	303.15	1571.4
0.8504	308.15	1550.5
0.8504	313.15	1529.7
0.8979	293.15	1639.1
0.8979	298.15	1617.5
0.8979	303.15	1596.1
0.8979	308.15	1574.8
0.8979	313.15	1553.1
0.9360	293.15	1660.5
0.9360	298.15	1638.7
0.9360	303.15	1616.8
0.9360	308.15	1595.3
0.9360	313.15	1573.7

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
0.0528	293.15	1279.7
0.0528	298.15	1262.9
0.0528	303.15	1245.9
0.0528	308.15	1228.5
0.0528	313.15	1210.7
0.1135	293.15	1302.1
0.1135	298.15	1285.0
0.1135	303.15	1267.9
0.1135	308.15	1250.7
0.1135	313.15	1233.6
0.1488	293.15	1315.9
0.1488	298.15	1298.6
0.1488	303.15	1281.4
0.1488	308.15	1264.3
0.1488	313.15	1247.2
0.2140	293.15	1341.7
0.2140	298.15	1324.3
0.2140	303.15	1306.8
0.2140	308.15	1289.5
0.2140	313.15	1272.3
0.2602	293.15	1360.5
0.2602	298.15	1342.9
0.2602	303.15	1325.3
0.2602	308.15	1307.8
0.2602	313.15	1290.4
0.3286	293.15	1387.1
0.3286	298.15	1368.8
0.3286	303.15	1350.9
0.3286	308.15	1333.6
0.3286	313.15	1315.8
0.3985	293.15	1414.5
0.3985	298.15	1396.3
0.3985	303.15	1378.1
0.3985	308.15	1360.0
0.3985	313.15	1341.9
0.5036	293.15	1456.5
0.5036	298.15	1437.7
0.5036	303.15	1419.1
0.5036	308.15	1400.4
0.5036	313.15	1381.7
0.5965	293.15	1494.7
0.5965	298.15	1475.5
0.5965	303.15	1456.3
0.5965	308.15	1437.1
0.5965	313.15	1418.1
0.7081	293.15	1543.9
0.7081	298.15	1523.9
0.7081	303.15	1504.0
0.7081	308.15	1484.2
0.7081	313.15	1464.4
0.7931	293.15	1584.7
0.7931	298.15	1564.1
0.7931	303.15	1543.5
0.7931	308.15	1523.0
0.7931	313.15	1502.7
0.8504	293.15	1613.6
0.8504	298.15	1592.5
0.8504	303.15	1571.4
0.8504	308.15	1550.5
0.8504	313.15	1529.7
0.8979	293.15	1639.1
0.8979	298.15	1617.5
0.8979	303.15	1596.1
0.8979	308.15	1574.8
0.8979	313.15	1553.1
0.9360	293.15	1660.5
0.9360	298.15	1638.7
0.9360	303.15	1616.8
0.9360	308.15	1595.3
0.9360	313.15	1573.7

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