Mixture of Tetrahydropyran + Butane, 1-chloro-

Datasets

1. Mole fraction (2)
2. ν - Kinematic viscosity, m2/s (2)
3. ρ_l - Mass density, kg/m3 (2)
4. γ - Surface tension liquid-gas, N/m (2)
5. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Tetrahydropyran (1) [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Tetrahydropyran (1) - Gas
0.0627	101.30	0.0443
0.0636	40.00	0.0434
0.1032	101.30	0.0748
0.1289	40.00	0.0890
0.1477	101.30	0.1062
0.1877	40.00	0.1398
0.2321	101.30	0.1749
0.2843	40.00	0.2161
0.3121	101.30	0.2494
0.3758	101.30	0.3090
0.4068	40.00	0.3294
0.4550	101.30	0.3834
0.4946	40.00	0.4117
0.5432	101.30	0.4749
0.5967	40.00	0.5317
0.6866	101.30	0.6311
0.6916	40.00	0.6308
0.7811	40.00	0.7296
0.8006	101.30	0.7564
0.8548	40.00	0.8207
0.8960	101.30	0.8712
0.9141	40.00	0.8959
0.9447	101.30	0.9321
0.9780	101.30	0.9736

Mole fraction of Tetrahydropyran (1) [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Tetrahydropyran (1) - Gas
0.0627	101.30	0.0443
0.0636	40.00	0.0434
0.1032	101.30	0.0748
0.1289	40.00	0.0890
0.1477	101.30	0.1062
0.1877	40.00	0.1398
0.2321	101.30	0.1749
0.2843	40.00	0.2161
0.3121	101.30	0.2494
0.3758	101.30	0.3090
0.4068	40.00	0.3294
0.4550	101.30	0.3834
0.4946	40.00	0.4117
0.5432	101.30	0.4749
0.5967	40.00	0.5317
0.6866	101.30	0.6311
0.6916	40.00	0.6308
0.7811	40.00	0.7296
0.8006	101.30	0.7564
0.8548	40.00	0.8207
0.8960	101.30	0.8712
0.9141	40.00	0.8959
0.9447	101.30	0.9321
0.9780	101.30	0.9736

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Kinematic viscosity, m2/s - Liquid
298.15	0.0000	4.7830e-07
298.15	0.0243	4.8350e-07
298.15	0.1039	5.0230e-07
298.15	0.2058	5.2930e-07
298.15	0.3070	5.5900e-07
298.15	0.3984	5.8880e-07
298.15	0.5077	6.2960e-07
298.15	0.6038	6.6850e-07
298.15	0.7064	7.1760e-07
298.15	0.7994	7.6820e-07
298.15	0.9058	8.3740e-07
298.15	0.9498	8.6980e-07
298.15	1.0000	9.1000e-07
313.15	0.0000	4.2140e-07
313.15	0.0243	4.2760e-07
313.15	0.1039	4.4180e-07
313.15	0.2058	4.6290e-07
313.15	0.3070	4.8550e-07
313.15	0.3984	5.0900e-07
313.15	0.5077	5.4040e-07
313.15	0.6038	5.7170e-07
313.15	0.7064	6.1010e-07
313.15	0.7994	6.4890e-07
313.15	0.9058	7.0100e-07
313.15	0.9498	7.2500e-07
313.15	1.0000	7.5710e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Kinematic viscosity, m2/s - Liquid
298.15	0.0000	4.7830e-07
298.15	0.0243	4.8350e-07
298.15	0.1039	5.0230e-07
298.15	0.2058	5.2930e-07
298.15	0.3070	5.5900e-07
298.15	0.3984	5.8880e-07
298.15	0.5077	6.2960e-07
298.15	0.6038	6.6850e-07
298.15	0.7064	7.1760e-07
298.15	0.7994	7.6820e-07
298.15	0.9058	8.3740e-07
298.15	0.9498	8.6980e-07
298.15	1.0000	9.1000e-07
313.15	0.0000	4.2140e-07
313.15	0.0243	4.2760e-07
313.15	0.1039	4.4180e-07
313.15	0.2058	4.6290e-07
313.15	0.3070	4.8550e-07
313.15	0.3984	5.0900e-07
313.15	0.5077	5.4040e-07
313.15	0.6038	5.7170e-07
313.15	0.7064	6.1010e-07
313.15	0.7994	6.4890e-07
313.15	0.9058	7.0100e-07
313.15	0.9498	7.2500e-07
313.15	1.0000	7.5710e-07

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	880.69
298.15	0.0521	880.67
298.15	0.1006	880.66
298.15	0.1949	880.62
298.15	0.2549	880.59
298.15	0.3774	880.48
298.15	0.5035	880.26
298.15	0.5948	880.06
298.15	0.6610	879.87
298.15	0.7893	879.49
298.15	0.9203	879.07
298.15	0.9666	878.91
298.15	1.0000	878.81
313.15	0.0000	863.82
313.15	0.0348	863.98
313.15	0.0899	864.19
313.15	0.1717	864.39
313.15	0.2933	864.54
313.15	0.4130	864.6
313.15	0.4926	864.61
313.15	0.6026	864.59
313.15	0.7085	864.52
313.15	0.8006	864.45
313.15	0.8990	864.22
313.15	0.9724	863.88
313.15	1.0000	863.67

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	880.69
298.15	0.0521	880.67
298.15	0.1006	880.66
298.15	0.1949	880.62
298.15	0.2549	880.59
298.15	0.3774	880.48
298.15	0.5035	880.26
298.15	0.5948	880.06
298.15	0.6610	879.87
298.15	0.7893	879.49
298.15	0.9203	879.07
298.15	0.9666	878.91
298.15	1.0000	878.81
313.15	0.0000	863.82
313.15	0.0348	863.98
313.15	0.0899	864.19
313.15	0.1717	864.39
313.15	0.2933	864.54
313.15	0.4130	864.6
313.15	0.4926	864.61
313.15	0.6026	864.59
313.15	0.7085	864.52
313.15	0.8006	864.45
313.15	0.8990	864.22
313.15	0.9724	863.88
313.15	1.0000	863.67

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0421	0.0234
298.15	0.1082	0.0237
298.15	0.2121	0.0240
298.15	0.3174	0.0244
298.15	0.4245	0.0248
298.15	0.5222	0.0252
298.15	0.6243	0.0256
298.15	0.7209	0.0260
298.15	0.8105	0.0264
298.15	0.9103	0.0269
298.15	0.9655	0.0271
313.15	0.0319	0.0217
313.15	0.1092	0.0220
313.15	0.2080	0.0223
313.15	0.3137	0.0227
313.15	0.4209	0.0230
313.15	0.5149	0.0234
313.15	0.6199	0.0238
313.15	0.7170	0.0242
313.15	0.8126	0.0246
313.15	0.9067	0.0250
313.15	0.9650	0.0252

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0421	0.0234
298.15	0.1082	0.0237
298.15	0.2121	0.0240
298.15	0.3174	0.0244
298.15	0.4245	0.0248
298.15	0.5222	0.0252
298.15	0.6243	0.0256
298.15	0.7209	0.0260
298.15	0.8105	0.0264
298.15	0.9103	0.0269
298.15	0.9655	0.0271
313.15	0.0319	0.0217
313.15	0.1092	0.0220
313.15	0.2080	0.0223
313.15	0.3137	0.0227
313.15	0.4209	0.0230
313.15	0.5149	0.0234
313.15	0.6199	0.0238
313.15	0.7170	0.0242
313.15	0.8126	0.0246
313.15	0.9067	0.0250
313.15	0.9650	0.0252

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0627	101.30	352.21
0.0636	40.00	324.95
0.1032	101.30	352.49
0.1289	40.00	325.53
0.1477	101.30	352.96
0.1877	40.00	326.15
0.2321	101.30	353.75
0.2843	40.00	327.05
0.3121	101.30	354.80
0.3758	101.30	355.49
0.4068	40.00	328.25
0.4550	101.30	356.35
0.4946	40.00	329.05
0.5432	101.30	357.02
0.5967	40.00	330.05
0.6866	101.30	358.58
0.6916	40.00	330.92
0.7811	40.00	331.71
0.8006	101.30	359.61
0.8548	40.00	332.25
0.8960	101.30	360.40
0.9141	40.00	332.81
0.9447	101.30	360.79
0.9780	101.30	361.18

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0627	101.30	352.21
0.0636	40.00	324.95
0.1032	101.30	352.49
0.1289	40.00	325.53
0.1477	101.30	352.96
0.1877	40.00	326.15
0.2321	101.30	353.75
0.2843	40.00	327.05
0.3121	101.30	354.80
0.3758	101.30	355.49
0.4068	40.00	328.25
0.4550	101.30	356.35
0.4946	40.00	329.05
0.5432	101.30	357.02
0.5967	40.00	330.05
0.6866	101.30	358.58
0.6916	40.00	330.92
0.7811	40.00	331.71
0.8006	101.30	359.61
0.8548	40.00	332.25
0.8960	101.30	360.40
0.9141	40.00	332.81
0.9447	101.30	360.79
0.9780	101.30	361.18

Sources

• Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
• Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
• Study of tetrahydropyran-chlorobutane VLE using the a o and o o approaches