Mixture of Tetrahydropyran + Butane, 2-chloro-

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Tetrahydropyran

Name
Tetrahydropyran
InChI
InChI=1S/C5H10O/c1-2-4-6-5-3-1/h1-5H2
InChI Key
DHXVGJBLRPWPCS-UHFFFAOYSA-N
Formula
C5H10O
SMILES
C1CCOCC1
Mol. Weight (g/mol)
86.13
CAS
142-68-7

Butane, 2-chloro-

Name
Butane, 2-chloro-
InChI
InChI=1S/C4H9Cl/c1-3-4(2)5/h4H,3H2,1-2H3
InChI Key
BSPCSKHALVHRSR-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CCC(C)Cl
Mol. Weight (g/mol)
92.57
CAS
78-86-4
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Datasets

  1. Mole fraction (2)
  2. ν - Kinematic viscosity, m2/s (2)
  3. ρl - Mass density, kg/m3 (2)
  4. γ - Surface tension liquid-gas, N/m (2)
  5. Tboil - 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