Mixture of Hexane, 1-chloro- + Tetrahydrofuran

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (2)
3. ν - Kinematic viscosity, m2/s (2)
4. P_vap - Vapor or sublimation pressure, kPa (2)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (4)
7. c_sound,fluid - Speed of Sound, m/s (2)
8. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Tetrahydrofuran (2) [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Pressure, kPa - Gas	Mole fraction of Tetrahydrofuran (2) - Gas
0.0251	101.33	0.1177
0.0313	40.00	0.1657
0.0637	101.33	0.2706
0.0696	40.00	0.3282
0.1025	40.00	0.4303
0.1082	101.33	0.4001
0.2045	101.33	0.6135
0.2227	40.00	0.6866
0.2486	40.00	0.7288
0.2705	101.33	0.7143
0.2812	101.33	0.7258
0.2903	40.00	0.7847
0.3197	40.00	0.8087
0.3298	101.33	0.7736
0.3549	101.33	0.7975
0.3577	40.00	0.8443
0.4039	101.33	0.8343
0.4278	40.00	0.8748
0.4649	40.00	0.9064
0.4696	101.33	0.8730
0.5599	101.33	0.9157
0.5619	40.00	0.9300
0.6694	40.00	0.9590
0.6719	101.33	0.9488
0.7310	101.33	0.9625
0.7318	40.00	0.9714
0.8479	101.33	0.9812
0.8600	40.00	0.9837
0.9163	40.00	0.9967
0.9163	101.33	0.9909

Mole fraction of Tetrahydrofuran (2) [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Gas	Mole fraction of Tetrahydrofuran (2) - Gas
0.0410	298.15	0.3092
0.0420	328.15	0.2500
0.0716	298.15	0.4622
0.0775	328.15	0.3912
0.0968	298.15	0.5514
0.1397	328.15	0.5728
0.1542	298.15	0.7112
0.1960	328.15	0.6844
0.1994	298.15	0.7771
0.2565	328.15	0.7723
0.2690	298.15	0.8461
0.3604	328.15	0.8624
0.3765	298.15	0.9042
0.4191	328.15	0.8840
0.4555	298.15	0.9317
0.4934	328.15	0.9152
0.5099	298.15	0.9468
0.5528	298.15	0.9560
0.5688	328.15	0.9422
0.6351	298.15	0.9685
0.6351	328.15	0.9529
0.7050	298.15	0.9793
0.7089	328.15	0.9675
0.7847	328.15	0.9803
0.7881	298.15	0.9880
0.8600	328.15	0.9919
0.8612	298.15	0.9938
0.9338	328.15	0.9976
0.9349	298.15	0.9995

Mole fraction of Tetrahydrofuran (2) [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Pressure, kPa - Gas	Mole fraction of Tetrahydrofuran (2) - Gas
0.0251	101.33	0.1177
0.0313	40.00	0.1657
0.0637	101.33	0.2706
0.0696	40.00	0.3282
0.1025	40.00	0.4303
0.1082	101.33	0.4001
0.2045	101.33	0.6135
0.2227	40.00	0.6866
0.2486	40.00	0.7288
0.2705	101.33	0.7143
0.2812	101.33	0.7258
0.2903	40.00	0.7847
0.3197	40.00	0.8087
0.3298	101.33	0.7736
0.3549	101.33	0.7975
0.3577	40.00	0.8443
0.4039	101.33	0.8343
0.4278	40.00	0.8748
0.4649	40.00	0.9064
0.4696	101.33	0.8730
0.5599	101.33	0.9157
0.5619	40.00	0.9300
0.6694	40.00	0.9590
0.6719	101.33	0.9488
0.7310	101.33	0.9625
0.7318	40.00	0.9714
0.8479	101.33	0.9812
0.8600	40.00	0.9837
0.9163	40.00	0.9967
0.9163	101.33	0.9909

Mole fraction of Tetrahydrofuran (2) [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Gas	Mole fraction of Tetrahydrofuran (2) - Gas
0.0410	298.15	0.3092
0.0420	328.15	0.2500
0.0716	298.15	0.4622
0.0775	328.15	0.3912
0.0968	298.15	0.5514
0.1397	328.15	0.5728
0.1542	298.15	0.7112
0.1960	328.15	0.6844
0.1994	298.15	0.7771
0.2565	328.15	0.7723
0.2690	298.15	0.8461
0.3604	328.15	0.8624
0.3765	298.15	0.9042
0.4191	328.15	0.8840
0.4555	298.15	0.9317
0.4934	328.15	0.9152
0.5099	298.15	0.9468
0.5528	298.15	0.9560
0.5688	328.15	0.9422
0.6351	298.15	0.9685
0.6351	328.15	0.9529
0.7050	298.15	0.9793
0.7089	328.15	0.9675
0.7847	328.15	0.9803
0.7881	298.15	0.9880
0.8600	328.15	0.9919
0.8612	298.15	0.9938
0.9338	328.15	0.9976
0.9349	298.15	0.9995

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Viscosity, Pa*s - Liquid
0.1039	0.0006
0.3050	0.0006
0.5025	0.0006
0.7336	0.0005
0.9013	0.0005

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Viscosity, Pa*s - Liquid
0.1039	0.0006
0.3050	0.0006
0.5025	0.0006
0.7336	0.0005
0.9013	0.0005

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0000	9.4780e-07
283.15	0.0571	9.3360e-07
283.15	0.1017	9.2260e-07
283.15	0.2025	8.9530e-07
283.15	0.2991	8.6700e-07
283.15	0.3981	8.3760e-07
283.15	0.4990	8.0540e-07
283.15	0.6041	7.6940e-07
283.15	0.6992	7.3440e-07
283.15	0.7977	6.9540e-07
283.15	0.8975	6.5340e-07
283.15	0.9497	6.3030e-07
283.15	1.0000	6.0770e-07
298.15	0.0000	7.9480e-07
298.15	0.0571	7.8400e-07
298.15	0.1017	7.7510e-07
298.15	0.2025	7.5340e-07
298.15	0.2991	7.3230e-07
298.15	0.3981	7.0880e-07
298.15	0.4990	6.8310e-07
298.15	0.6041	6.5460e-07
298.15	0.6992	6.2640e-07
298.15	0.7977	5.9590e-07
298.15	0.8975	5.6200e-07
298.15	0.9497	5.4310e-07
298.15	1.0000	5.2510e-07
313.15	0.0000	6.7660e-07
313.15	0.0571	6.6780e-07
313.15	0.1017	6.6070e-07
313.15	0.2025	6.4350e-07
313.15	0.2991	6.2670e-07
313.15	0.3981	6.0800e-07
313.15	0.4990	5.8710e-07
313.15	0.6041	5.6400e-07
313.15	0.6992	5.4120e-07
313.15	0.7977	5.1620e-07
313.15	0.8975	4.8850e-07
313.15	0.9497	4.7390e-07
313.15	1.0000	4.5980e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0000	9.4780e-07
283.15	0.0571	9.3360e-07
283.15	0.1017	9.2260e-07
283.15	0.2025	8.9530e-07
283.15	0.2991	8.6700e-07
283.15	0.3981	8.3760e-07
283.15	0.4990	8.0540e-07
283.15	0.6041	7.6940e-07
283.15	0.6992	7.3440e-07
283.15	0.7977	6.9540e-07
283.15	0.8975	6.5340e-07
283.15	0.9497	6.3030e-07
283.15	1.0000	6.0770e-07
298.15	0.0000	7.9480e-07
298.15	0.0571	7.8400e-07
298.15	0.1017	7.7510e-07
298.15	0.2025	7.5340e-07
298.15	0.2991	7.3230e-07
298.15	0.3981	7.0880e-07
298.15	0.4990	6.8310e-07
298.15	0.6041	6.5460e-07
298.15	0.6992	6.2640e-07
298.15	0.7977	5.9590e-07
298.15	0.8975	5.6200e-07
298.15	0.9497	5.4310e-07
298.15	1.0000	5.2510e-07
313.15	0.0000	6.7660e-07
313.15	0.0571	6.6780e-07
313.15	0.1017	6.6070e-07
313.15	0.2025	6.4350e-07
313.15	0.2991	6.2670e-07
313.15	0.3981	6.0800e-07
313.15	0.4990	5.8710e-07
313.15	0.6041	5.6400e-07
313.15	0.6992	5.4120e-07
313.15	0.7977	5.1620e-07
313.15	0.8975	4.8850e-07
313.15	0.9497	4.7390e-07
313.15	1.0000	4.5980e-07

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0410	298.15	1.70
0.0420	328.15	7.49
0.0716	298.15	2.09
0.0775	328.15	8.97
0.0968	298.15	2.46
0.1397	328.15	12.36
0.1542	298.15	3.50
0.1960	328.15	15.48
0.1994	298.15	4.33
0.2565	328.15	19.14
0.2690	298.15	5.79
0.3604	328.15	25.82
0.3765	298.15	8.02
0.4191	328.15	30.09
0.4555	298.15	9.77
0.4934	328.15	35.38
0.5099	298.15	10.90
0.5528	298.15	11.93
0.5688	328.15	40.61
0.6351	298.15	13.61
0.6351	328.15	45.42
0.7050	298.15	15.37
0.7089	328.15	50.62
0.7847	328.15	55.91
0.7881	298.15	17.23
0.8600	328.15	61.12
0.8612	298.15	18.76
0.9338	328.15	66.14
0.9349	298.15	20.27

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0410	298.15	1.70
0.0420	328.15	7.49
0.0716	298.15	2.09
0.0775	328.15	8.97
0.0968	298.15	2.46
0.1397	328.15	12.36
0.1542	298.15	3.50
0.1960	328.15	15.48
0.1994	298.15	4.33
0.2565	328.15	19.14
0.2690	298.15	5.79
0.3604	328.15	25.82
0.3765	298.15	8.02
0.4191	328.15	30.09
0.4555	298.15	9.77
0.4934	328.15	35.38
0.5099	298.15	10.90
0.5528	298.15	11.93
0.5688	328.15	40.61
0.6351	298.15	13.61
0.6351	328.15	45.42
0.7050	298.15	15.37
0.7089	328.15	50.62
0.7847	328.15	55.91
0.7881	298.15	17.23
0.8600	328.15	61.12
0.8612	298.15	18.76
0.9338	328.15	66.14
0.9349	298.15	20.27

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Refractive index (Na D-line) - Liquid
0.1039	1.4161
0.3050	1.4142
0.5025	1.4122
0.7336	1.4088
0.9013	1.4053

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Refractive index (Na D-line) - Liquid
0.1039	1.4161
0.3050	1.4142
0.5025	1.4122
0.7336	1.4088
0.9013	1.4053

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Mass density, kg/m3 - Liquid
0.1039	869.11
0.3050	870.03
0.5025	871.36
0.7336	873.79
0.9013	875.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	887.11
283.15	0.0571	887.43
283.15	0.1017	887.71
283.15	0.2025	888.42
283.15	0.2991	889.16
283.15	0.3981	889.92
283.15	0.4990	890.86
283.15	0.6041	891.99
283.15	0.6992	893.11
283.15	0.7977	894.45
283.15	0.8975	896.08
283.15	0.9497	897.03
283.15	1.0000	897.98
298.15	0.0000	873.55
298.15	0.0571	873.72
298.15	0.1017	873.95
298.15	0.2025	874.44
298.15	0.2991	874.91
298.15	0.3981	875.56
298.15	0.4990	876.3
298.15	0.6041	877.18
298.15	0.6992	878.19
298.15	0.7977	879.17
298.15	0.8975	880.43
298.15	0.9497	881.24
298.15	1.0000	881.93
313.15	0.0000	859.0
313.15	0.0571	859.09
313.15	0.1017	859.24
313.15	0.2025	859.52
313.15	0.2991	859.9
313.15	0.3981	860.36
313.15	0.4990	861.01
313.15	0.6041	861.7
313.15	0.6992	862.34
313.15	0.7977	863.23
313.15	0.8975	864.28
313.15	0.9497	864.74
313.15	1.0000	865.38

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Mass density, kg/m3 - Liquid
0.1039	869.11
0.3050	870.03
0.5025	871.36
0.7336	873.79
0.9013	875.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	887.11
283.15	0.0571	887.43
283.15	0.1017	887.71
283.15	0.2025	888.42
283.15	0.2991	889.16
283.15	0.3981	889.92
283.15	0.4990	890.86
283.15	0.6041	891.99
283.15	0.6992	893.11
283.15	0.7977	894.45
283.15	0.8975	896.08
283.15	0.9497	897.03
283.15	1.0000	897.98
298.15	0.0000	873.55
298.15	0.0571	873.72
298.15	0.1017	873.95
298.15	0.2025	874.44
298.15	0.2991	874.91
298.15	0.3981	875.56
298.15	0.4990	876.3
298.15	0.6041	877.18
298.15	0.6992	878.19
298.15	0.7977	879.17
298.15	0.8975	880.43
298.15	0.9497	881.24
298.15	1.0000	881.93
313.15	0.0000	859.0
313.15	0.0571	859.09
313.15	0.1017	859.24
313.15	0.2025	859.52
313.15	0.2991	859.9
313.15	0.3981	860.36
313.15	0.4990	861.01
313.15	0.6041	861.7
313.15	0.6992	862.34
313.15	0.7977	863.23
313.15	0.8975	864.28
313.15	0.9497	864.74
313.15	1.0000	865.38

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Speed of sound, m/s - Liquid
0.1039	1195.0
0.3050	1216.0
0.5025	1233.0
0.7336	1247.0
0.9013	1252.0

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Speed of sound, m/s - Liquid
0.1039	1195.0
0.3050	1216.0
0.5025	1233.0
0.7336	1247.0
0.9013	1252.0

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.33	408.07
0.0251	101.33	405.51
0.0313	40.00	373.20
0.0637	101.33	399.04
0.0696	40.00	367.47
0.1025	40.00	363.25
0.1082	101.33	392.86
0.2045	101.33	383.04
0.2227	40.00	350.89
0.2486	40.00	348.07
0.2705	101.33	375.84
0.2812	101.33	375.11
0.2903	40.00	344.55
0.3197	40.00	342.72
0.3298	101.33	370.85
0.3549	101.33	369.17
0.3577	40.00	339.65
0.4039	101.33	365.97
0.4278	40.00	335.72
0.4649	40.00	333.03
0.4696	101.33	361.66
0.5599	101.33	356.41
0.5619	40.00	327.89
0.6694	40.00	323.86
0.6719	101.33	351.05
0.7310	101.33	348.45
0.7318	40.00	321.26
0.8479	101.33	344.11
0.8600	40.00	316.82
0.9163	40.00	315.73
0.9163	101.33	341.83
1.0000	101.33	339.12

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.33	408.07
0.0251	101.33	405.51
0.0313	40.00	373.20
0.0637	101.33	399.04
0.0696	40.00	367.47
0.1025	40.00	363.25
0.1082	101.33	392.86
0.2045	101.33	383.04
0.2227	40.00	350.89
0.2486	40.00	348.07
0.2705	101.33	375.84
0.2812	101.33	375.11
0.2903	40.00	344.55
0.3197	40.00	342.72
0.3298	101.33	370.85
0.3549	101.33	369.17
0.3577	40.00	339.65
0.4039	101.33	365.97
0.4278	40.00	335.72
0.4649	40.00	333.03
0.4696	101.33	361.66
0.5599	101.33	356.41
0.5619	40.00	327.89
0.6694	40.00	323.86
0.6719	101.33	351.05
0.7310	101.33	348.45
0.7318	40.00	321.26
0.8479	101.33	344.11
0.8600	40.00	316.82
0.9163	40.00	315.73
0.9163	101.33	341.83
1.0000	101.33	339.12

Sources

• Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
• Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
• Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
• Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K