Mixture of 1,3-Dioxolane + Pentane, 1-chloro-

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 1,3-Dioxolane (1) [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0000	298.15	0.0000
0.0000	313.15	0.0000
0.0000	328.15	0.0000
0.0595	313.15	0.2366
0.0596	328.15	0.2142
0.0602	298.15	0.2526
0.1130	328.15	0.3394
0.1132	313.15	0.3667
0.1190	298.15	0.3841
0.2041	313.15	0.5237
0.2058	328.15	0.5013
0.2224	298.15	0.5601
0.3240	328.15	0.6430
0.3393	298.15	0.6741
0.3453	313.15	0.6658
0.4025	298.15	0.7215
0.4075	313.15	0.7148
0.4547	313.15	0.7616
0.4617	328.15	0.7430
0.4679	298.15	0.7656
0.5567	328.15	0.7956
0.5764	313.15	0.8180
0.5780	298.15	0.8232
0.6244	298.15	0.8410
0.6255	328.15	0.8240
0.6285	313.15	0.8379
0.7209	328.15	0.8723
0.7219	313.15	0.8853
0.7249	298.15	0.8803
0.7832	313.15	0.9009
0.7874	328.15	0.8988
0.7886	298.15	0.9021
0.8383	328.15	0.9210
0.8957	313.15	0.9455
0.8959	328.15	0.9452
0.8964	298.15	0.9449
0.9458	298.15	0.9685
0.9458	313.15	0.9687
0.9469	328.15	0.9693
1.0000	298.15	1.0000
1.0000	313.15	1.0000
1.0000	328.15	1.0000

Mole fraction of 1,3-Dioxolane (1) [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0000	298.15	0.0000
0.0000	313.15	0.0000
0.0000	328.15	0.0000
0.0595	313.15	0.2366
0.0596	328.15	0.2142
0.0602	298.15	0.2526
0.1130	328.15	0.3394
0.1132	313.15	0.3667
0.1190	298.15	0.3841
0.2041	313.15	0.5237
0.2058	328.15	0.5013
0.2224	298.15	0.5601
0.3240	328.15	0.6430
0.3393	298.15	0.6741
0.3453	313.15	0.6658
0.4025	298.15	0.7215
0.4075	313.15	0.7148
0.4547	313.15	0.7616
0.4617	328.15	0.7430
0.4679	298.15	0.7656
0.5567	328.15	0.7956
0.5764	313.15	0.8180
0.5780	298.15	0.8232
0.6244	298.15	0.8410
0.6255	328.15	0.8240
0.6285	313.15	0.8379
0.7209	328.15	0.8723
0.7219	313.15	0.8853
0.7249	298.15	0.8803
0.7832	313.15	0.9009
0.7874	328.15	0.8988
0.7886	298.15	0.9021
0.8383	328.15	0.9210
0.8957	313.15	0.9455
0.8959	328.15	0.9452
0.8964	298.15	0.9449
0.9458	298.15	0.9685
0.9458	313.15	0.9687
0.9469	328.15	0.9693
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 1,3-Dioxolane (1) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0000	7.3160e-07
283.15	0.0503	7.2410e-07
283.15	0.1013	7.1900e-07
283.15	0.1939	7.0870e-07
283.15	0.2965	6.9850e-07
283.15	0.3968	6.8940e-07
283.15	0.4993	6.8130e-07
283.15	0.5995	6.7450e-07
283.15	0.6973	6.6760e-07
283.15	0.7986	6.6220e-07
283.15	0.8997	6.5710e-07
283.15	0.9498	6.5550e-07
283.15	1.0000	6.5290e-07
298.15	0.0000	6.2790e-07
298.15	0.0503	6.2180e-07
298.15	0.1013	6.1670e-07
298.15	0.1939	6.0720e-07
298.15	0.2965	5.9750e-07
298.15	0.3968	5.8930e-07
298.15	0.4993	5.8170e-07
298.15	0.5995	5.7490e-07
298.15	0.6973	5.6860e-07
298.15	0.7986	5.6380e-07
298.15	0.8997	5.5870e-07
298.15	0.9498	5.5820e-07
298.15	1.0000	5.5590e-07
313.15	0.0000	5.4210e-07
313.15	0.0503	5.3670e-07
313.15	0.1013	5.3170e-07
313.15	0.1939	5.2350e-07
313.15	0.2965	5.1540e-07
313.15	0.3968	5.0740e-07
313.15	0.4993	5.0050e-07
313.15	0.5995	4.9430e-07
313.15	0.6973	4.8980e-07
313.15	0.7986	4.8510e-07
313.15	0.8997	4.8120e-07
313.15	0.9498	4.8000e-07
313.15	1.0000	4.7840e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0000	7.3160e-07
283.15	0.0503	7.2410e-07
283.15	0.1013	7.1900e-07
283.15	0.1939	7.0870e-07
283.15	0.2965	6.9850e-07
283.15	0.3968	6.8940e-07
283.15	0.4993	6.8130e-07
283.15	0.5995	6.7450e-07
283.15	0.6973	6.6760e-07
283.15	0.7986	6.6220e-07
283.15	0.8997	6.5710e-07
283.15	0.9498	6.5550e-07
283.15	1.0000	6.5290e-07
298.15	0.0000	6.2790e-07
298.15	0.0503	6.2180e-07
298.15	0.1013	6.1670e-07
298.15	0.1939	6.0720e-07
298.15	0.2965	5.9750e-07
298.15	0.3968	5.8930e-07
298.15	0.4993	5.8170e-07
298.15	0.5995	5.7490e-07
298.15	0.6973	5.6860e-07
298.15	0.7986	5.6380e-07
298.15	0.8997	5.5870e-07
298.15	0.9498	5.5820e-07
298.15	1.0000	5.5590e-07
313.15	0.0000	5.4210e-07
313.15	0.0503	5.3670e-07
313.15	0.1013	5.3170e-07
313.15	0.1939	5.2350e-07
313.15	0.2965	5.1540e-07
313.15	0.3968	5.0740e-07
313.15	0.4993	5.0050e-07
313.15	0.5995	4.9430e-07
313.15	0.6973	4.8980e-07
313.15	0.7986	4.8510e-07
313.15	0.8997	4.8120e-07
313.15	0.9498	4.8000e-07
313.15	1.0000	4.7840e-07

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - 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
0.0595	313.15	10.42
0.0596	328.15	19.64
0.0602	298.15	5.10
0.1130	328.15	22.19
0.1132	313.15	12.06
0.1190	298.15	6.06
0.2041	313.15	14.53
0.2058	328.15	26.63
0.2224	298.15	7.40
0.3240	328.15	31.30
0.3393	298.15	8.85
0.3453	313.15	17.57
0.4025	298.15	9.41
0.4075	313.15	18.89
0.4547	313.15	19.73
0.4617	328.15	35.95
0.4679	298.15	10.05
0.5567	328.15	38.76
0.5764	313.15	21.55
0.5780	298.15	10.90
0.6244	298.15	11.28
0.6255	328.15	40.66
0.6285	313.15	22.34
0.7209	328.15	43.00
0.7219	313.15	23.66
0.7249	298.15	11.91
0.7832	313.15	24.43
0.7874	328.15	44.44
0.7886	298.15	12.25
0.8383	328.15	45.59
0.8957	313.15	25.72
0.8959	328.15	46.84
0.8964	298.15	12.95
0.9458	298.15	13.24
0.9458	313.15	26.29
0.9469	328.15	47.92
1.0000	298.15	13.54
1.0000	313.15	26.83
1.0000	328.15	49.01

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - 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
0.0595	313.15	10.42
0.0596	328.15	19.64
0.0602	298.15	5.10
0.1130	328.15	22.19
0.1132	313.15	12.06
0.1190	298.15	6.06
0.2041	313.15	14.53
0.2058	328.15	26.63
0.2224	298.15	7.40
0.3240	328.15	31.30
0.3393	298.15	8.85
0.3453	313.15	17.57
0.4025	298.15	9.41
0.4075	313.15	18.89
0.4547	313.15	19.73
0.4617	328.15	35.95
0.4679	298.15	10.05
0.5567	328.15	38.76
0.5764	313.15	21.55
0.5780	298.15	10.90
0.6244	298.15	11.28
0.6255	328.15	40.66
0.6285	313.15	22.34
0.7209	328.15	43.00
0.7219	313.15	23.66
0.7249	298.15	11.91
0.7832	313.15	24.43
0.7874	328.15	44.44
0.7886	298.15	12.25
0.8383	328.15	45.59
0.8957	313.15	25.72
0.8959	328.15	46.84
0.8964	298.15	12.95
0.9458	298.15	13.24
0.9458	313.15	26.29
0.9469	328.15	47.92
1.0000	298.15	13.54
1.0000	313.15	26.83
1.0000	328.15	49.01

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	892.29
283.15	0.0503	897.25
283.15	0.1013	902.36
283.15	0.1939	913.36
283.15	0.2965	925.84
283.15	0.3968	940.53
283.15	0.4993	956.85
283.15	0.5995	975.09
283.15	0.6973	995.06
283.15	0.7986	1018.88
283.15	0.8997	1045.96
283.15	0.9498	1061.33
283.15	1.0000	1077.65
298.15	0.0000	877.05
298.15	0.0503	881.96
298.15	0.1013	887.14
298.15	0.1939	897.4
298.15	0.2965	910.13
298.15	0.3968	924.15
298.15	0.4993	940.35
298.15	0.5995	958.08
298.15	0.6973	977.84
298.15	0.7986	1000.89
298.15	0.8997	1027.56
298.15	0.9498	1042.46
298.15	1.0000	1058.64
313.15	0.0000	861.46
313.15	0.0503	866.22
313.15	0.1013	871.36
313.15	0.1939	881.57
313.15	0.2965	893.87
313.15	0.3968	907.37
313.15	0.4993	922.88
313.15	0.5995	940.32
313.15	0.6973	959.58
313.15	0.7986	982.68
313.15	0.8997	1009.56
313.15	0.9498	1024.17
313.15	1.0000	1039.92

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	892.29
283.15	0.0503	897.25
283.15	0.1013	902.36
283.15	0.1939	913.36
283.15	0.2965	925.84
283.15	0.3968	940.53
283.15	0.4993	956.85
283.15	0.5995	975.09
283.15	0.6973	995.06
283.15	0.7986	1018.88
283.15	0.8997	1045.96
283.15	0.9498	1061.33
283.15	1.0000	1077.65
298.15	0.0000	877.05
298.15	0.0503	881.96
298.15	0.1013	887.14
298.15	0.1939	897.4
298.15	0.2965	910.13
298.15	0.3968	924.15
298.15	0.4993	940.35
298.15	0.5995	958.08
298.15	0.6973	977.84
298.15	0.7986	1000.89
298.15	0.8997	1027.56
298.15	0.9498	1042.46
298.15	1.0000	1058.64
313.15	0.0000	861.46
313.15	0.0503	866.22
313.15	0.1013	871.36
313.15	0.1939	881.57
313.15	0.2965	893.87
313.15	0.3968	907.37
313.15	0.4993	922.88
313.15	0.5995	940.32
313.15	0.6973	959.58
313.15	0.7986	982.68
313.15	0.8997	1009.56
313.15	0.9498	1024.17
313.15	1.0000	1039.92

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