Mixture of Tetrahydropyran + Propane, 1-chloro-2-methyl-

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
0.0670	40.00	0.0402
0.0690	101.30	0.0361
0.1696	40.00	0.0839
0.1808	101.30	0.1039
0.2024	40.00	0.1067
0.2694	101.30	0.1666
0.2920	40.00	0.1703
0.4095	101.30	0.2764
0.4317	40.00	0.2747
0.4705	101.30	0.3305
0.5604	40.00	0.3967
0.6145	40.00	0.4591
0.6876	101.30	0.5647
0.6876	101.30	0.5647
0.6878	40.00	0.5391
0.7244	101.30	0.6010
0.7789	40.00	0.6513
0.8408	101.30	0.7540
0.8616	40.00	0.7724
0.9030	101.30	0.8481
0.9313	40.00	0.8816
0.9622	101.30	0.9308

Mole fraction of Tetrahydropyran (1) [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Tetrahydropyran (1) - Gas
0.0670	40.00	0.0402
0.0690	101.30	0.0361
0.1696	40.00	0.0839
0.1808	101.30	0.1039
0.2024	40.00	0.1067
0.2694	101.30	0.1666
0.2920	40.00	0.1703
0.4095	101.30	0.2764
0.4317	40.00	0.2747
0.4705	101.30	0.3305
0.5604	40.00	0.3967
0.6145	40.00	0.4591
0.6876	101.30	0.5647
0.6876	101.30	0.5647
0.6878	40.00	0.5391
0.7244	101.30	0.6010
0.7789	40.00	0.6513
0.8408	101.30	0.7540
0.8616	40.00	0.7724
0.9030	101.30	0.8481
0.9313	40.00	0.8816
0.9622	101.30	0.9308

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	4.9300e-07
298.15	0.0540	5.0630e-07
298.15	0.1069	5.1930e-07
298.15	0.2033	5.4570e-07
298.15	0.3110	5.7760e-07
298.15	0.4126	6.1120e-07
298.15	0.5040	6.4450e-07
298.15	0.5950	6.8160e-07
298.15	0.6954	7.2700e-07
298.15	0.8028	7.8260e-07
298.15	0.9066	8.4640e-07
298.15	0.9578	8.7970e-07
298.15	1.0000	9.1000e-07
313.15	0.0000	4.2920e-07
313.15	0.0540	4.3980e-07
313.15	0.1069	4.5090e-07
313.15	0.2033	4.7180e-07
313.15	0.3110	4.9670e-07
313.15	0.4126	5.2310e-07
313.15	0.5040	5.5020e-07
313.15	0.5950	5.7960e-07
313.15	0.6954	6.1560e-07
313.15	0.8028	6.6050e-07
313.15	0.9066	7.0680e-07
313.15	0.9578	7.3320e-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	4.9300e-07
298.15	0.0540	5.0630e-07
298.15	0.1069	5.1930e-07
298.15	0.2033	5.4570e-07
298.15	0.3110	5.7760e-07
298.15	0.4126	6.1120e-07
298.15	0.5040	6.4450e-07
298.15	0.5950	6.8160e-07
298.15	0.6954	7.2700e-07
298.15	0.8028	7.8260e-07
298.15	0.9066	8.4640e-07
298.15	0.9578	8.7970e-07
298.15	1.0000	9.1000e-07
313.15	0.0000	4.2920e-07
313.15	0.0540	4.3980e-07
313.15	0.1069	4.5090e-07
313.15	0.2033	4.7180e-07
313.15	0.3110	4.9670e-07
313.15	0.4126	5.2310e-07
313.15	0.5040	5.5020e-07
313.15	0.5950	5.7960e-07
313.15	0.6954	6.1560e-07
313.15	0.8028	6.6050e-07
313.15	0.9066	7.0680e-07
313.15	0.9578	7.3320e-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	871.13
298.15	0.0480	871.69
298.15	0.1084	872.39
298.15	0.2120	873.53
298.15	0.2900	874.38
298.15	0.3951	875.37
298.15	0.5062	876.3
298.15	0.6273	877.23
298.15	0.6897	877.63
298.15	0.8111	878.26
298.15	0.9088	878.68
298.15	0.9520	878.79
298.15	1.0000	878.81
313.15	0.0000	853.51
313.15	0.0432	854.17
313.15	0.0934	854.93
313.15	0.1923	856.35
313.15	0.3025	857.83
313.15	0.4060	859.08
313.15	0.5018	860.14
313.15	0.6079	861.19
313.15	0.7238	862.24
313.15	0.7895	862.78
313.15	0.8874	863.42
313.15	0.9463	863.68
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	871.13
298.15	0.0480	871.69
298.15	0.1084	872.39
298.15	0.2120	873.53
298.15	0.2900	874.38
298.15	0.3951	875.37
298.15	0.5062	876.3
298.15	0.6273	877.23
298.15	0.6897	877.63
298.15	0.8111	878.26
298.15	0.9088	878.68
298.15	0.9520	878.79
298.15	1.0000	878.81
313.15	0.0000	853.51
313.15	0.0432	854.17
313.15	0.0934	854.93
313.15	0.1923	856.35
313.15	0.3025	857.83
313.15	0.4060	859.08
313.15	0.5018	860.14
313.15	0.6079	861.19
313.15	0.7238	862.24
313.15	0.7895	862.78
313.15	0.8874	863.42
313.15	0.9463	863.68
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	0.0483	0.0222
298.15	0.1067	0.0226
298.15	0.2075	0.0231
298.15	0.3200	0.0236
298.15	0.4148	0.0241
298.15	0.5190	0.0246
298.15	0.6219	0.0251
298.15	0.7194	0.0256
298.15	0.8079	0.0261
298.15	0.9077	0.0267
298.15	0.9602	0.0270
313.15	0.0377	0.0196
313.15	0.1032	0.0201
313.15	0.2167	0.0209
313.15	0.3226	0.0216
313.15	0.4213	0.0221
313.15	0.5302	0.0227
313.15	0.6241	0.0233
313.15	0.7134	0.0238
313.15	0.8148	0.0244
313.15	0.9051	0.0249
313.15	0.9660	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	0.0483	0.0222
298.15	0.1067	0.0226
298.15	0.2075	0.0231
298.15	0.3200	0.0236
298.15	0.4148	0.0241
298.15	0.5190	0.0246
298.15	0.6219	0.0251
298.15	0.7194	0.0256
298.15	0.8079	0.0261
298.15	0.9077	0.0267
298.15	0.9602	0.0270
313.15	0.0377	0.0196
313.15	0.1032	0.0201
313.15	0.2167	0.0209
313.15	0.3226	0.0216
313.15	0.4213	0.0221
313.15	0.5302	0.0227
313.15	0.6241	0.0233
313.15	0.7134	0.0238
313.15	0.8148	0.0244
313.15	0.9051	0.0249
313.15	0.9660	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
0.0670	40.00	316.27
0.0690	101.30	343.14
0.1696	40.00	317.76
0.1808	101.30	345.00
0.2024	40.00	318.45
0.2694	101.30	346.49
0.2920	40.00	319.71
0.4095	101.30	348.92
0.4317	40.00	322.26
0.4705	101.30	350.30
0.5604	40.00	324.40
0.6145	40.00	325.43
0.6876	101.30	354.32
0.6876	101.30	354.32
0.6878	40.00	326.87
0.7244	101.30	355.15
0.7789	40.00	328.68
0.8408	101.30	357.61
0.8616	40.00	330.34
0.9030	101.30	359.04
0.9313	40.00	331.90
0.9622	101.30	360.49

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
0.0670	40.00	316.27
0.0690	101.30	343.14
0.1696	40.00	317.76
0.1808	101.30	345.00
0.2024	40.00	318.45
0.2694	101.30	346.49
0.2920	40.00	319.71
0.4095	101.30	348.92
0.4317	40.00	322.26
0.4705	101.30	350.30
0.5604	40.00	324.40
0.6145	40.00	325.43
0.6876	101.30	354.32
0.6876	101.30	354.32
0.6878	40.00	326.87
0.7244	101.30	355.15
0.7789	40.00	328.68
0.8408	101.30	357.61
0.8616	40.00	330.34
0.9030	101.30	359.04
0.9313	40.00	331.90
0.9622	101.30	360.49

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