Mixture of 1-Butanol + Ethylbenzene

Datasets

1. Activity coefficient (8)
2. Mole fraction (2)
3. η - Viscosity, Pa*s (2)
4. ρ_l - Mass density, kg/m3 (2)
5. c_sound,fluid - Speed of Sound, m/s (2)
6. T_boil - Boiling temperature at pressure P, K (2)

Activity coefficient of 1-Butanol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
303.15	11.8
313.15	9.49
323.15	7.63

Activity coefficient of 1-Butanol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
398.15	2.55
409.15	2.24

Activity coefficient of Ethylbenzene (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Activity coefficient of Ethylbenzene (2) - Liquid
323.15	0.0000	3.84

(Relative) activity of Ethylbenzene (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	(Relative) activity of Ethylbenzene (2) - Liquid
363.15	3.24
373.15	3.05
383.15	2.78
390.15	2.67

Activity coefficient of 1-Butanol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
303.15	11.8
313.15	9.49
323.15	7.63

Activity coefficient of 1-Butanol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
398.15	2.55
409.15	2.24

Activity coefficient of Ethylbenzene (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Activity coefficient of Ethylbenzene (2) - Liquid
323.15	0.0000	3.84

(Relative) activity of Ethylbenzene (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	(Relative) activity of Ethylbenzene (2) - Liquid
363.15	3.24
373.15	3.05
383.15	2.78
390.15	2.67

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Gas)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0000	0.0000
0.0386	0.1472
0.0635	0.2167
0.1118	0.3033
0.1637	0.3804
0.2288	0.4561
0.2862	0.4932
0.4272	0.5764
0.4911	0.6089
0.5732	0.6468
0.6033	0.6647
0.6546	0.6965
0.7031	0.7163
0.7438	0.7410
0.7992	0.7899
0.8415	0.8159
0.8966	0.8662
0.9450	0.9283
0.9820	0.9763
1.0000	1.0000

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Gas)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0000	0.0000
0.0386	0.1472
0.0635	0.2167
0.1118	0.3033
0.1637	0.3804
0.2288	0.4561
0.2862	0.4932
0.4272	0.5764
0.4911	0.6089
0.5732	0.6468
0.6033	0.6647
0.6546	0.6965
0.7031	0.7163
0.7438	0.7410
0.7992	0.7899
0.8415	0.8159
0.8966	0.8662
0.9450	0.9283
0.9820	0.9763
1.0000	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0026
298.15	0.1035	0.0020
298.15	0.2050	0.0016
298.15	0.3221	0.0012
298.15	0.3650	0.0011
298.15	0.5071	0.0009
298.15	0.6494	0.0008
298.15	0.8136	0.0007
298.15	0.9100	0.0006
298.15	1.0000	0.0006
308.15	0.0000	0.0020
308.15	0.1035	0.0016
308.15	0.2050	0.0013
308.15	0.3221	0.0011
308.15	0.3650	0.0009
308.15	0.5071	0.0008
308.15	0.6494	0.0007
308.15	0.8136	0.0006
308.15	0.9100	0.0006
308.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0026
298.15	0.1035	0.0020
298.15	0.2050	0.0016
298.15	0.3221	0.0012
298.15	0.3650	0.0011
298.15	0.5071	0.0009
298.15	0.6494	0.0008
298.15	0.8136	0.0007
298.15	0.9100	0.0006
298.15	1.0000	0.0006
308.15	0.0000	0.0020
308.15	0.1035	0.0016
308.15	0.2050	0.0013
308.15	0.3221	0.0011
308.15	0.3650	0.0009
308.15	0.5071	0.0008
308.15	0.6494	0.0007
308.15	0.8136	0.0006
308.15	0.9100	0.0006
308.15	1.0000	0.0006

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	807.7
298.15	0.1035	816.7
298.15	0.2050	821.2
298.15	0.3221	828.1
298.15	0.3650	831.1
298.15	0.5071	839.6
298.15	0.6494	845.7
298.15	0.8136	854.5
298.15	0.9100	858.6
298.15	1.0000	862.0
308.15	0.0000	800.1
308.15	0.1035	808.9
308.15	0.2050	815.3
308.15	0.3221	822.0
308.15	0.3650	824.5
308.15	0.5071	832.1
308.15	0.6494	839.1
308.15	0.8136	846.0
308.15	0.9100	852.6
308.15	1.0000	855.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	807.7
298.15	0.1035	816.7
298.15	0.2050	821.2
298.15	0.3221	828.1
298.15	0.3650	831.1
298.15	0.5071	839.6
298.15	0.6494	845.7
298.15	0.8136	854.5
298.15	0.9100	858.6
298.15	1.0000	862.0
308.15	0.0000	800.1
308.15	0.1035	808.9
308.15	0.2050	815.3
308.15	0.3221	822.0
308.15	0.3650	824.5
308.15	0.5071	832.1
308.15	0.6494	839.1
308.15	0.8136	846.0
308.15	0.9100	852.6
308.15	1.0000	855.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1238.0
298.15	0.1035	1246.0
298.15	0.2050	1256.0
298.15	0.3221	1264.0
298.15	0.3650	1267.0
298.15	0.5071	1277.0
298.15	0.6494	1288.0
298.15	0.8136	1301.0
298.15	0.9100	1307.0
298.15	1.0000	1312.0
308.15	0.0000	1211.0
308.15	0.1035	1217.0
308.15	0.2050	1223.0
308.15	0.3221	1229.0
308.15	0.3650	1231.0
308.15	0.5071	1239.0
308.15	0.6494	1249.0
308.15	0.8136	1262.0
308.15	0.9100	1268.0
308.15	1.0000	1276.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1238.0
298.15	0.1035	1246.0
298.15	0.2050	1256.0
298.15	0.3221	1264.0
298.15	0.3650	1267.0
298.15	0.5071	1277.0
298.15	0.6494	1288.0
298.15	0.8136	1301.0
298.15	0.9100	1307.0
298.15	1.0000	1312.0
308.15	0.0000	1211.0
308.15	0.1035	1217.0
308.15	0.2050	1223.0
308.15	0.3221	1229.0
308.15	0.3650	1231.0
308.15	0.5071	1239.0
308.15	0.6494	1249.0
308.15	0.8136	1262.0
308.15	0.9100	1268.0
308.15	1.0000	1276.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	409.27
0.0386	404.97
0.0635	402.83
0.1118	399.62
0.1637	396.81
0.2288	394.27
0.2862	392.49
0.4272	390.81
0.4911	390.30
0.5732	390.05
0.6033	389.74
0.6546	389.49
0.7031	389.34
0.7438	389.28
0.7992	389.38
0.8415	389.49
0.8966	389.79
0.9450	390.30
0.9820	390.70
1.0000	390.85

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	409.27
0.0386	404.97
0.0635	402.83
0.1118	399.62
0.1637	396.81
0.2288	394.27
0.2862	392.49
0.4272	390.81
0.4911	390.30
0.5732	390.05
0.6033	389.74
0.6546	389.49
0.7031	389.34
0.7438	389.28
0.7992	389.38
0.8415	389.49
0.8966	389.79
0.9450	390.30
0.9820	390.70
1.0000	390.85

Sources

• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Viscosities, Densities, and Ultrasonic Velocities of Binary Mixtures of Ethylbenzene with Ethanol, 1-Propanol, and 1-Butanol at (298.15 and 308.15)K
• Isobaric vapor liquid equilibium for the binary systerms of 1-butanol with o-xylene, m-xylene, p-xylene, and ethylbenzene at 101.33 kPa