Mixture of Pentane, 1-chloro- + Tetrahydrofuran

Datasets

1. Mole fraction (2)
2. ν - Kinematic viscosity, m2/s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Tetrahydrofuran (2) [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0000	298.15	0.0000
0.0000	313.15	0.0000
0.0000	328.15	0.0000
0.0765	313.15	0.2268
0.0765	328.15	0.2089
0.0800	298.15	0.2422
0.1381	298.15	0.3857
0.1450	313.15	0.3727
0.1479	328.15	0.3630
0.2100	298.15	0.5227
0.2101	313.15	0.5001
0.2101	328.15	0.4759
0.2745	328.15	0.5713
0.2813	313.15	0.6087
0.2903	298.15	0.6362
0.3645	328.15	0.6863
0.3762	313.15	0.7116
0.3915	298.15	0.7554
0.4418	328.15	0.7534
0.4468	313.15	0.7825
0.4644	298.15	0.8110
0.5200	313.15	0.8346
0.5200	328.15	0.8198
0.5201	298.15	0.8479
0.5724	328.15	0.8520
0.5798	313.15	0.8705
0.6042	298.15	0.9007
0.6686	328.15	0.9056
0.6727	313.15	0.9195
0.7099	298.15	0.9372
0.7943	313.15	0.9516
0.7955	298.15	0.9593
0.7962	328.15	0.9525
0.8665	328.15	0.9715
0.8700	298.15	0.9854
0.8711	313.15	0.9749
0.9687	313.15	0.9948
0.9696	298.15	0.9950
0.9700	328.15	0.9942
1.0000	298.15	1.0000
1.0000	313.15	1.0000
1.0000	328.15	1.0000

Mole fraction of Tetrahydrofuran (2) [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0000	298.15	0.0000
0.0000	313.15	0.0000
0.0000	328.15	0.0000
0.0765	313.15	0.2268
0.0765	328.15	0.2089
0.0800	298.15	0.2422
0.1381	298.15	0.3857
0.1450	313.15	0.3727
0.1479	328.15	0.3630
0.2100	298.15	0.5227
0.2101	313.15	0.5001
0.2101	328.15	0.4759
0.2745	328.15	0.5713
0.2813	313.15	0.6087
0.2903	298.15	0.6362
0.3645	328.15	0.6863
0.3762	313.15	0.7116
0.3915	298.15	0.7554
0.4418	328.15	0.7534
0.4468	313.15	0.7825
0.4644	298.15	0.8110
0.5200	313.15	0.8346
0.5200	328.15	0.8198
0.5201	298.15	0.8479
0.5724	328.15	0.8520
0.5798	313.15	0.8705
0.6042	298.15	0.9007
0.6686	328.15	0.9056
0.6727	313.15	0.9195
0.7099	298.15	0.9372
0.7943	313.15	0.9516
0.7955	298.15	0.9593
0.7962	328.15	0.9525
0.8665	328.15	0.9715
0.8700	298.15	0.9854
0.8711	313.15	0.9749
0.9687	313.15	0.9948
0.9696	298.15	0.9950
0.9700	328.15	0.9942
1.0000	298.15	1.0000
1.0000	313.15	1.0000
1.0000	328.15	1.0000

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	7.3160e-07
283.15	0.0628	7.2610e-07
283.15	0.1041	7.2230e-07
283.15	0.2093	7.1260e-07
283.15	0.3101	7.0290e-07
283.15	0.3988	6.9350e-07
283.15	0.4742	6.8480e-07
283.15	0.5957	6.7040e-07
283.15	0.6958	6.5710e-07
283.15	0.8013	6.4190e-07
283.15	0.8982	6.2670e-07
283.15	0.9456	6.1810e-07
283.15	1.0000	6.0770e-07
298.15	0.0000	6.2790e-07
298.15	0.0628	6.2310e-07
298.15	0.1041	6.2000e-07
298.15	0.2093	6.1240e-07
298.15	0.3101	6.0370e-07
298.15	0.3988	5.9580e-07
298.15	0.4742	5.8870e-07
298.15	0.5957	5.7630e-07
298.15	0.6958	5.6540e-07
298.15	0.8013	5.5320e-07
298.15	0.8982	5.3990e-07
298.15	0.9456	5.3350e-07
298.15	1.0000	5.2510e-07
313.15	0.0000	5.4210e-07
313.15	0.0628	5.3860e-07
313.15	0.1041	5.3590e-07
313.15	0.2093	5.2930e-07
313.15	0.3101	5.2230e-07
313.15	0.3988	5.1580e-07
313.15	0.4742	5.1000e-07
313.15	0.5957	4.9980e-07
313.15	0.6958	4.9100e-07
313.15	0.8013	4.8080e-07
313.15	0.8982	4.7060e-07
313.15	0.9456	4.6530e-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	7.3160e-07
283.15	0.0628	7.2610e-07
283.15	0.1041	7.2230e-07
283.15	0.2093	7.1260e-07
283.15	0.3101	7.0290e-07
283.15	0.3988	6.9350e-07
283.15	0.4742	6.8480e-07
283.15	0.5957	6.7040e-07
283.15	0.6958	6.5710e-07
283.15	0.8013	6.4190e-07
283.15	0.8982	6.2670e-07
283.15	0.9456	6.1810e-07
283.15	1.0000	6.0770e-07
298.15	0.0000	6.2790e-07
298.15	0.0628	6.2310e-07
298.15	0.1041	6.2000e-07
298.15	0.2093	6.1240e-07
298.15	0.3101	6.0370e-07
298.15	0.3988	5.9580e-07
298.15	0.4742	5.8870e-07
298.15	0.5957	5.7630e-07
298.15	0.6958	5.6540e-07
298.15	0.8013	5.5320e-07
298.15	0.8982	5.3990e-07
298.15	0.9456	5.3350e-07
298.15	1.0000	5.2510e-07
313.15	0.0000	5.4210e-07
313.15	0.0628	5.3860e-07
313.15	0.1041	5.3590e-07
313.15	0.2093	5.2930e-07
313.15	0.3101	5.2230e-07
313.15	0.3988	5.1580e-07
313.15	0.4742	5.1000e-07
313.15	0.5957	4.9980e-07
313.15	0.6958	4.9100e-07
313.15	0.8013	4.8080e-07
313.15	0.8982	4.7060e-07
313.15	0.9456	4.6530e-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
0.0000	298.15	4.05
0.0000	313.15	8.45
0.0000	328.15	16.40
0.0765	313.15	10.03
0.0765	328.15	19.12
0.0800	298.15	5.00
0.1381	298.15	5.67
0.1450	313.15	11.62
0.1479	328.15	21.91
0.2100	298.15	6.62
0.2101	313.15	13.24
0.2101	328.15	24.47
0.2745	328.15	27.38
0.2813	313.15	15.17
0.2903	298.15	7.75
0.3645	328.15	31.60
0.3762	313.15	17.85
0.3915	298.15	9.32
0.4418	328.15	35.70
0.4468	313.15	20.14
0.4644	298.15	10.61
0.5200	313.15	22.52
0.5200	328.15	40.06
0.5201	298.15	11.59
0.5724	328.15	43.15
0.5798	313.15	24.59
0.6042	298.15	13.22
0.6686	328.15	49.12
0.6727	313.15	28.01
0.7099	298.15	15.39
0.7943	313.15	32.72
0.7955	298.15	17.26
0.7962	328.15	57.37
0.8665	328.15	62.09
0.8700	298.15	18.87
0.8711	313.15	35.74
0.9687	313.15	39.49
0.9696	298.15	20.92
0.9700	328.15	68.68
1.0000	298.15	21.61
1.0000	313.15	40.62
1.0000	328.15	70.61

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	298.15	4.05
0.0000	313.15	8.45
0.0000	328.15	16.40
0.0765	313.15	10.03
0.0765	328.15	19.12
0.0800	298.15	5.00
0.1381	298.15	5.67
0.1450	313.15	11.62
0.1479	328.15	21.91
0.2100	298.15	6.62
0.2101	313.15	13.24
0.2101	328.15	24.47
0.2745	328.15	27.38
0.2813	313.15	15.17
0.2903	298.15	7.75
0.3645	328.15	31.60
0.3762	313.15	17.85
0.3915	298.15	9.32
0.4418	328.15	35.70
0.4468	313.15	20.14
0.4644	298.15	10.61
0.5200	313.15	22.52
0.5200	328.15	40.06
0.5201	298.15	11.59
0.5724	328.15	43.15
0.5798	313.15	24.59
0.6042	298.15	13.22
0.6686	328.15	49.12
0.6727	313.15	28.01
0.7099	298.15	15.39
0.7943	313.15	32.72
0.7955	298.15	17.26
0.7962	328.15	57.37
0.8665	328.15	62.09
0.8700	298.15	18.87
0.8711	313.15	35.74
0.9687	313.15	39.49
0.9696	298.15	20.92
0.9700	328.15	68.68
1.0000	298.15	21.61
1.0000	313.15	40.62
1.0000	328.15	70.61

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	892.29
283.15	0.0628	892.58
283.15	0.1041	892.84
283.15	0.2093	893.49
283.15	0.3101	894.01
283.15	0.3988	894.45
283.15	0.4742	895.01
283.15	0.5957	895.73
283.15	0.6958	896.36
283.15	0.8013	896.87
283.15	0.8982	897.4
283.15	0.9456	897.75
283.15	1.0000	897.98
298.15	0.0000	877.05
298.15	0.0628	877.23
298.15	0.1041	877.42
298.15	0.2093	877.86
298.15	0.3101	878.25
298.15	0.3988	878.65
298.15	0.4742	878.89
298.15	0.5957	879.58
298.15	0.6958	880.08
298.15	0.8013	880.69
298.15	0.8982	881.27
298.15	0.9456	881.54
298.15	1.0000	881.93
313.15	0.0000	861.46
313.15	0.0628	861.68
313.15	0.1041	861.73
313.15	0.2093	862.08
313.15	0.3101	862.34
313.15	0.3988	862.54
313.15	0.4742	862.94
313.15	0.5957	863.35
313.15	0.6958	863.75
313.15	0.8013	864.18
313.15	0.8982	864.85
313.15	0.9456	865.03
313.15	1.0000	865.38

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	892.29
283.15	0.0628	892.58
283.15	0.1041	892.84
283.15	0.2093	893.49
283.15	0.3101	894.01
283.15	0.3988	894.45
283.15	0.4742	895.01
283.15	0.5957	895.73
283.15	0.6958	896.36
283.15	0.8013	896.87
283.15	0.8982	897.4
283.15	0.9456	897.75
283.15	1.0000	897.98
298.15	0.0000	877.05
298.15	0.0628	877.23
298.15	0.1041	877.42
298.15	0.2093	877.86
298.15	0.3101	878.25
298.15	0.3988	878.65
298.15	0.4742	878.89
298.15	0.5957	879.58
298.15	0.6958	880.08
298.15	0.8013	880.69
298.15	0.8982	881.27
298.15	0.9456	881.54
298.15	1.0000	881.93
313.15	0.0000	861.46
313.15	0.0628	861.68
313.15	0.1041	861.73
313.15	0.2093	862.08
313.15	0.3101	862.34
313.15	0.3988	862.54
313.15	0.4742	862.94
313.15	0.5957	863.35
313.15	0.6958	863.75
313.15	0.8013	864.18
313.15	0.8982	864.85
313.15	0.9456	865.03
313.15	1.0000	865.38

Sources

• Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
• Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K