Mixture of Tetrahydropyran + Butane, 2-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
0.0615	40.00	0.0272
0.0713	101.30	0.0312
0.1288	40.00	0.0638
0.1496	101.30	0.0864
0.2116	40.00	0.1134
0.2503	101.30	0.1503
0.3167	40.00	0.1871
0.3766	101.30	0.2486
0.4098	40.00	0.2481
0.4868	101.30	0.3436
0.5143	40.00	0.3521
0.5818	101.30	0.4377
0.6547	40.00	0.4885
0.7082	101.30	0.5816
0.7100	40.00	0.5588
0.7662	40.00	0.6266
0.8088	40.00	0.6871
0.8147	101.30	0.7185
0.8755	101.30	0.8029
0.8963	40.00	0.8138
0.9271	101.30	0.8855
0.9635	101.30	0.9381

Mole fraction of Tetrahydropyran (1) [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Tetrahydropyran (1) - Gas
0.0615	40.00	0.0272
0.0713	101.30	0.0312
0.1288	40.00	0.0638
0.1496	101.30	0.0864
0.2116	40.00	0.1134
0.2503	101.30	0.1503
0.3167	40.00	0.1871
0.3766	101.30	0.2486
0.4098	40.00	0.2481
0.4868	101.30	0.3436
0.5143	40.00	0.3521
0.5818	101.30	0.4377
0.6547	40.00	0.4885
0.7082	101.30	0.5816
0.7100	40.00	0.5588
0.7662	40.00	0.6266
0.8088	40.00	0.6871
0.8147	101.30	0.7185
0.8755	101.30	0.8029
0.8963	40.00	0.8138
0.9271	101.30	0.8855
0.9635	101.30	0.9381

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	4.5400e-07
298.15	0.0605	4.6570e-07
298.15	0.1166	4.8050e-07
298.15	0.2131	5.0810e-07
298.15	0.3174	5.4250e-07
298.15	0.4088	5.7510e-07
298.15	0.4994	6.1110e-07
298.15	0.6122	6.6200e-07
298.15	0.7108	7.1360e-07
298.15	0.8059	7.6870e-07
298.15	0.9023	8.3360e-07
298.15	0.9549	8.7290e-07
298.15	1.0000	9.1000e-07
313.15	0.0000	3.9650e-07
313.15	0.0605	4.0930e-07
313.15	0.1166	4.2200e-07
313.15	0.2131	4.4540e-07
313.15	0.3174	4.7200e-07
313.15	0.4088	4.9710e-07
313.15	0.4994	5.2530e-07
313.15	0.6122	5.6560e-07
313.15	0.7108	6.0590e-07
313.15	0.8059	6.4850e-07
313.15	0.9023	6.9750e-07
313.15	0.9549	7.2800e-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	4.5400e-07
298.15	0.0605	4.6570e-07
298.15	0.1166	4.8050e-07
298.15	0.2131	5.0810e-07
298.15	0.3174	5.4250e-07
298.15	0.4088	5.7510e-07
298.15	0.4994	6.1110e-07
298.15	0.6122	6.6200e-07
298.15	0.7108	7.1360e-07
298.15	0.8059	7.6870e-07
298.15	0.9023	8.3360e-07
298.15	0.9549	8.7290e-07
298.15	1.0000	9.1000e-07
313.15	0.0000	3.9650e-07
313.15	0.0605	4.0930e-07
313.15	0.1166	4.2200e-07
313.15	0.2131	4.4540e-07
313.15	0.3174	4.7200e-07
313.15	0.4088	4.9710e-07
313.15	0.4994	5.2530e-07
313.15	0.6122	5.6560e-07
313.15	0.7108	6.0590e-07
313.15	0.8059	6.4850e-07
313.15	0.9023	6.9750e-07
313.15	0.9549	7.2800e-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	867.37
298.15	0.0525	868.05
298.15	0.1035	869.06
298.15	0.1947	870.26
298.15	0.3042	871.8
298.15	0.4091	872.95
298.15	0.5025	874.28
298.15	0.5947	875.42
298.15	0.7116	876.72
298.15	0.8090	877.46
298.15	0.8917	878.36
298.15	0.9599	878.55
298.15	1.0000	878.81
313.15	0.0000	850.13
313.15	0.0605	851.11
313.15	0.1166	852.02
313.15	0.2131	853.59
313.15	0.3174	855.4
313.15	0.4088	857.0
313.15	0.4994	858.35
313.15	0.6122	859.58
313.15	0.7108	861.03
313.15	0.8059	862.1
313.15	0.9023	862.9
313.15	0.9549	863.45
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	867.37
298.15	0.0525	868.05
298.15	0.1035	869.06
298.15	0.1947	870.26
298.15	0.3042	871.8
298.15	0.4091	872.95
298.15	0.5025	874.28
298.15	0.5947	875.42
298.15	0.7116	876.72
298.15	0.8090	877.46
298.15	0.8917	878.36
298.15	0.9599	878.55
298.15	1.0000	878.81
313.15	0.0000	850.13
313.15	0.0605	851.11
313.15	0.1166	852.02
313.15	0.2131	853.59
313.15	0.3174	855.4
313.15	0.4088	857.0
313.15	0.4994	858.35
313.15	0.6122	859.58
313.15	0.7108	861.03
313.15	0.8059	862.1
313.15	0.9023	862.9
313.15	0.9549	863.45
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	0.0400	0.0221
298.15	0.1057	0.0224
298.15	0.2133	0.0229
298.15	0.3195	0.0234
298.15	0.4166	0.0239
298.15	0.5188	0.0244
298.15	0.6151	0.0250
298.15	0.7111	0.0256
298.15	0.8098	0.0261
298.15	0.9438	0.0270
298.15	0.9845	0.0272
313.15	0.0355	0.0196
313.15	0.1006	0.0200
313.15	0.2177	0.0208
313.15	0.3192	0.0215
313.15	0.4243	0.0221
313.15	0.5166	0.0227
313.15	0.5931	0.0231
313.15	0.7193	0.0238
313.15	0.8156	0.0243
313.15	0.9057	0.0249
313.15	0.9910	0.0253

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	0.0400	0.0221
298.15	0.1057	0.0224
298.15	0.2133	0.0229
298.15	0.3195	0.0234
298.15	0.4166	0.0239
298.15	0.5188	0.0244
298.15	0.6151	0.0250
298.15	0.7111	0.0256
298.15	0.8098	0.0261
298.15	0.9438	0.0270
298.15	0.9845	0.0272
313.15	0.0355	0.0196
313.15	0.1006	0.0200
313.15	0.2177	0.0208
313.15	0.3192	0.0215
313.15	0.4243	0.0221
313.15	0.5166	0.0227
313.15	0.5931	0.0231
313.15	0.7193	0.0238
313.15	0.8156	0.0243
313.15	0.9057	0.0249
313.15	0.9910	0.0253

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
0.0615	40.00	315.21
0.0713	101.30	342.51
0.1288	40.00	316.25
0.1496	101.30	343.88
0.2116	40.00	317.65
0.2503	101.30	345.85
0.3167	40.00	319.61
0.3766	101.30	348.25
0.4098	40.00	321.12
0.4868	101.30	350.53
0.5143	40.00	323.14
0.5818	101.30	352.53
0.6547	40.00	325.98
0.7082	101.30	355.24
0.7100	40.00	327.17
0.7662	40.00	328.12
0.8088	40.00	328.98
0.8147	101.30	357.35
0.8755	101.30	358.77
0.8963	40.00	331.15
0.9271	101.30	359.80
0.9635	101.30	360.57

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
0.0615	40.00	315.21
0.0713	101.30	342.51
0.1288	40.00	316.25
0.1496	101.30	343.88
0.2116	40.00	317.65
0.2503	101.30	345.85
0.3167	40.00	319.61
0.3766	101.30	348.25
0.4098	40.00	321.12
0.4868	101.30	350.53
0.5143	40.00	323.14
0.5818	101.30	352.53
0.6547	40.00	325.98
0.7082	101.30	355.24
0.7100	40.00	327.17
0.7662	40.00	328.12
0.8088	40.00	328.98
0.8147	101.30	357.35
0.8755	101.30	358.77
0.8963	40.00	331.15
0.9271	101.30	359.80
0.9635	101.30	360.57

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