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

Excel

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

Propane, 2-chloro-2-methyl-

Name
Propane, 2-chloro-2-methyl-
InChI
InChI=1S/C4H9Cl/c1-4(2,3)5/h1-3H3
InChI Key
NBRKLOOSMBRFMH-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CC(C)(C)Cl
Mol. Weight (g/mol)
92.57
CAS
507-20-0
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

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]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydropyran (1) - Liquid Mole fraction of Tetrahydropyran (1) - Gas
0.0766 0.0200
0.1427 0.0426
0.1949 0.0661
0.3188 0.1138
0.4038 0.1657
0.4554 0.2051
0.5560 0.2826
0.6007 0.3214
0.7247 0.4709
0.7789 0.5490
0.8742 0.7244
0.9235 0.8208
0.9781 0.9429

Mole fraction of Tetrahydropyran (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydropyran (1) - Liquid Mole fraction of Tetrahydropyran (1) - Gas
0.0766 0.0200
0.1427 0.0426
0.1949 0.0661
0.3188 0.1138
0.4038 0.1657
0.4554 0.2051
0.5560 0.2826
0.6007 0.3214
0.7247 0.4709
0.7789 0.5490
0.8742 0.7244
0.9235 0.8208
0.9781 0.9429

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 5.6800e-07
298.15 0.0614 5.8400e-07
298.15 0.1075 5.9610e-07
298.15 0.2173 6.2740e-07
298.15 0.3205 6.5700e-07
298.15 0.4200 6.8790e-07
298.15 0.5176 7.1980e-07
298.15 0.6155 7.5400e-07
298.15 0.7156 7.9080e-07
298.15 0.8277 8.3490e-07
298.15 0.9097 8.6990e-07
298.15 0.9547 8.8940e-07
298.15 1.0000 9.1000e-07
313.15 0.0000 4.7750e-07
313.15 0.0451 4.8720e-07
313.15 0.0887 4.9690e-07
313.15 0.1978 5.2090e-07
313.15 0.3053 5.4660e-07
313.15 0.3972 5.6990e-07
313.15 0.5024 5.9850e-07
313.15 0.6359 6.3630e-07
313.15 0.7056 6.5750e-07
313.15 0.7960 6.8590e-07
313.15 0.9063 7.2300e-07
313.15 0.9526 7.3970e-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 5.6800e-07
298.15 0.0614 5.8400e-07
298.15 0.1075 5.9610e-07
298.15 0.2173 6.2740e-07
298.15 0.3205 6.5700e-07
298.15 0.4200 6.8790e-07
298.15 0.5176 7.1980e-07
298.15 0.6155 7.5400e-07
298.15 0.7156 7.9080e-07
298.15 0.8277 8.3490e-07
298.15 0.9097 8.6990e-07
298.15 0.9547 8.8940e-07
298.15 1.0000 9.1000e-07
313.15 0.0000 4.7750e-07
313.15 0.0451 4.8720e-07
313.15 0.0887 4.9690e-07
313.15 0.1978 5.2090e-07
313.15 0.3053 5.4660e-07
313.15 0.3972 5.6990e-07
313.15 0.5024 5.9850e-07
313.15 0.6359 6.3630e-07
313.15 0.7056 6.5750e-07
313.15 0.7960 6.8590e-07
313.15 0.9063 7.2300e-07
313.15 0.9526 7.3970e-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 836.45
298.15 0.0324 838.08
298.15 0.1086 842.07
298.15 0.2097 847.11
298.15 0.2891 851.05
298.15 0.4276 857.41
298.15 0.4960 860.32
298.15 0.6107 864.98
298.15 0.6483 866.46
298.15 0.8093 872.39
298.15 0.8606 874.22
298.15 0.9540 877.25
298.15 1.0000 878.81
313.15 0.0000 818.31
313.15 0.0584 821.7
313.15 0.0875 823.35
313.15 0.1943 829.15
313.15 0.3028 834.83
313.15 0.4249 840.83
313.15 0.4929 843.99
313.15 0.6093 849.16
313.15 0.7052 853.15
313.15 0.7988 856.89
313.15 0.9097 860.95
313.15 0.9614 862.64
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 836.45
298.15 0.0324 838.08
298.15 0.1086 842.07
298.15 0.2097 847.11
298.15 0.2891 851.05
298.15 0.4276 857.41
298.15 0.4960 860.32
298.15 0.6107 864.98
298.15 0.6483 866.46
298.15 0.8093 872.39
298.15 0.8606 874.22
298.15 0.9540 877.25
298.15 1.0000 878.81
313.15 0.0000 818.31
313.15 0.0584 821.7
313.15 0.0875 823.35
313.15 0.1943 829.15
313.15 0.3028 834.83
313.15 0.4249 840.83
313.15 0.4929 843.99
313.15 0.6093 849.16
313.15 0.7052 853.15
313.15 0.7988 856.89
313.15 0.9097 860.95
313.15 0.9614 862.64
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 0.0332 0.0192
298.15 0.0955 0.0197
298.15 0.2242 0.0207
298.15 0.3219 0.0214
298.15 0.4336 0.0222
298.15 0.5374 0.0230
298.15 0.6269 0.0237
298.15 0.7173 0.0245
298.15 0.8149 0.0254
298.15 0.9089 0.0264
298.15 0.9418 0.0267
313.15 0.0734 0.0174
313.15 0.1038 0.0175
313.15 0.2093 0.0181
313.15 0.3169 0.0189
313.15 0.4363 0.0198
313.15 0.5116 0.0204
313.15 0.6120 0.0212
313.15 0.7058 0.0221
313.15 0.8154 0.0231
313.15 0.9006 0.0240
313.15 0.9529 0.0247

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 0.0332 0.0192
298.15 0.0955 0.0197
298.15 0.2242 0.0207
298.15 0.3219 0.0214
298.15 0.4336 0.0222
298.15 0.5374 0.0230
298.15 0.6269 0.0237
298.15 0.7173 0.0245
298.15 0.8149 0.0254
298.15 0.9089 0.0264
298.15 0.9418 0.0267
313.15 0.0734 0.0174
313.15 0.1038 0.0175
313.15 0.2093 0.0181
313.15 0.3169 0.0189
313.15 0.4363 0.0198
313.15 0.5116 0.0204
313.15 0.6120 0.0212
313.15 0.7058 0.0221
313.15 0.8154 0.0231
313.15 0.9006 0.0240
313.15 0.9529 0.0247

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydropyran (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0766 325.70
0.1427 327.21
0.1949 328.87
0.3188 332.69
0.4038 335.34
0.4554 337.15
0.5560 340.85
0.6007 342.61
0.7247 347.84
0.7789 350.30
0.8742 354.86
0.9235 357.35
0.9781 360.20

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydropyran (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0766 325.70
0.1427 327.21
0.1949 328.87
0.3188 332.69
0.4038 335.34
0.4554 337.15
0.5560 340.85
0.6007 342.61
0.7247 347.84
0.7789 350.30
0.8742 354.86
0.9235 357.35
0.9781 360.20

Sources