Mixture of 1-Propanol + Cyclohexane

Datasets

1. η - Viscosity, Pa*s (2)
2. Excess molar enthalpy (molar enthalpy
3. P_vap - Vapor or sublimation pressure, kPa
4. ρ_l - Mass density, kg/m3 (2)
5. c_sound,fluid - Speed of Sound, m/s
6. Binary diffusion coefficient, m2/s

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0008
0.1021	0.0008
0.2112	0.0009
0.3122	0.0009
0.4211	0.0010
0.5151	0.0011
0.6203	0.0011
0.7208	0.0013
0.8143	0.0014
0.9079	0.0016
1.0000	0.0017

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0022
293.15	0.0487	0.0021
293.15	0.0993	0.0020
293.15	0.1967	0.0017
293.15	0.2993	0.0015
293.15	0.4017	0.0014
293.15	0.5071	0.0013
293.15	0.6048	0.0011
293.15	0.7036	0.0010
293.15	0.8062	0.0010
293.15	0.9053	0.0010
293.15	0.9522	0.0010
293.15	1.0000	0.0010
298.15	0.0000	0.0019
298.15	0.0487	0.0018
298.15	0.0993	0.0017
298.15	0.1967	0.0015
298.15	0.2993	0.0014
298.15	0.4017	0.0012
298.15	0.5071	0.0011
298.15	0.6048	0.0010
298.15	0.7036	0.0009
298.15	0.8062	0.0009
298.15	0.9053	0.0009
298.15	0.9522	0.0009
298.15	1.0000	0.0009
303.15	0.0000	0.0017
303.15	0.0487	0.0016
303.15	0.0993	0.0016
303.15	0.1967	0.0014
303.15	0.2993	0.0012
303.15	0.4017	0.0011
303.15	0.5071	0.0010
303.15	0.6048	0.0009
303.15	0.7036	0.0009
303.15	0.8062	0.0008
303.15	0.9053	0.0008
303.15	0.9522	0.0008
303.15	1.0000	0.0008

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0503	0.0910
298.15	0.1005	0.1730
298.15	0.1499	0.2470
298.15	0.2005	0.3160
298.15	0.2499	0.3780
298.15	0.3005	0.4350
298.15	0.3503	0.4860
298.15	0.4003	0.5310
298.15	0.4501	0.5690
298.15	0.4998	0.5990
298.15	0.5504	0.6230
298.15	0.6006	0.6370
298.15	0.6503	0.6420
298.15	0.6995	0.6360
298.15	0.8005	0.5820
298.15	0.8497	0.5300
298.15	0.9005	0.4560
298.15	0.9502	0.3460
313.15	0.0503	0.1070
313.15	0.1005	0.2080
313.15	0.1499	0.3000
313.15	0.2005	0.3880
313.15	0.2498	0.4670
313.15	0.3004	0.5410
313.15	0.3502	0.6070
313.15	0.4001	0.6660
313.15	0.4500	0.7170
313.15	0.4997	0.7580
313.15	0.5502	0.7900
313.15	0.6006	0.8100
313.15	0.6503	0.8190
313.15	0.6994	0.8130
313.15	0.7503	0.7910
313.15	0.8005	0.7500
313.15	0.8497	0.6890
313.15	0.9005	0.5980
313.15	0.9502	0.4590

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.3999	303.39	15.10
0.3999	308.56	18.50
0.3999	313.42	22.30
0.3999	318.12	26.70
0.3999	323.18	31.60
0.3999	328.27	38.40
0.3999	333.26	45.60
0.3999	338.24	54.00
0.3999	343.17	64.10
0.9000	303.56	17.90
0.9000	308.37	21.80
0.9000	313.29	26.20
0.9000	318.28	31.60
0.9000	323.07	37.60
0.9000	328.25	45.40
0.9000	333.17	54.00
0.9000	338.26	63.70
0.9000	343.19	75.60

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	769.16
0.1021	769.52
0.2112	770.68
0.3122	772.37
0.4211	774.63
0.5151	776.9
0.6203	779.94
0.7208	783.15
0.8143	786.73
0.9079	790.83
1.0000	795.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	803.59
293.15	0.0487	801.17
293.15	0.0993	798.82
293.15	0.1967	794.76
293.15	0.2993	791.11
293.15	0.4017	787.98
293.15	0.5071	785.25
293.15	0.6048	783.08
293.15	0.7036	781.23
293.15	0.8062	779.66
293.15	0.9053	778.68
293.15	0.9522	778.41
293.15	1.0000	778.62
298.15	0.0000	799.58
298.15	0.0487	797.11
298.15	0.0993	794.71
298.15	0.1967	790.54
298.15	0.2993	786.78
298.15	0.4017	783.54
298.15	0.5071	780.71
298.15	0.6048	778.47
298.15	0.7036	776.55
298.15	0.8062	774.94
298.15	0.9053	773.93
298.15	0.9522	773.66
298.15	1.0000	773.92
303.15	0.0000	795.55
303.15	0.0487	793.02
303.15	0.0993	790.56
303.15	0.1967	786.28
303.15	0.2993	782.41
303.15	0.4017	779.05
303.15	0.5071	776.12
303.15	0.6048	773.8
303.15	0.7036	771.82
303.15	0.8062	770.17
303.15	0.9053	769.14
303.15	0.9522	768.87
303.15	1.0000	769.19

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1223.0
293.15	0.0487	1222.0
293.15	0.0993	1222.0
293.15	0.1967	1223.0
293.15	0.2993	1225.0
293.15	0.4017	1228.0
293.15	0.5071	1233.0
293.15	0.6048	1238.0
293.15	0.7036	1244.0
293.15	0.8062	1252.0
293.15	0.9053	1262.0
293.15	0.9522	1268.0
293.15	1.0000	1279.0
298.15	0.0000	1206.0
298.15	0.0487	1205.0
298.15	0.0993	1204.0
298.15	0.1967	1204.0
298.15	0.2993	1205.0
298.15	0.4017	1207.0
298.15	0.5071	1211.0
298.15	0.6048	1215.0
298.15	0.7036	1221.0
298.15	0.8062	1228.0
298.15	0.9053	1237.0
298.15	0.9522	1243.0
298.15	1.0000	1254.0
303.15	0.0000	1189.0
303.15	0.0487	1187.0
303.15	0.0993	1186.0
303.15	0.1967	1185.0
303.15	0.2993	1185.0
303.15	0.4017	1186.0
303.15	0.5071	1189.0
303.15	0.6048	1193.0
303.15	0.7036	1198.0
303.15	0.8062	1204.0
303.15	0.9053	1213.0
303.15	0.9522	1219.0
303.15	1.0000	1230.0

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0300	0.0000
0.1000	0.0000
0.3000	0.0000
0.5000	0.0000
0.7000	0.0000
0.9000	0.0000
0.9700	0.0000

Sources

• Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
• Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
• Excess enthalpies of ternary mixtures of (oxygenated additives + cycloalkane) in fuels and bio-fuels: (dibutyl ether + 1-propanol + cyclohexane), or methylcyclohexane, at T = (298.15 and 313.15) K
• Volumetric and transport properties of ternary mixtures containing 1-propanol, triethylamine or tri-n-butylamine and cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems

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