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

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Propane, 1-chloro-2-methyl-

Name
Propane, 1-chloro-2-methyl-
InChI
InChI=1S/C4H9Cl/c1-4(2)3-5/h4H,3H2,1-2H3
InChI Key
QTBFPMKWQKYFLR-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CC(C)CCl
Mol. Weight (g/mol)
92.57
CAS
513-36-0

Tetrahydrofuran

Name
Tetrahydrofuran
InChI
InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
InChI Key
WYURNTSHIVDZCO-UHFFFAOYSA-N
Formula
C4H8O
SMILES
C1CCOC1
Mol. Weight (g/mol)
72.11
CAS
109-99-9
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)
  3. γ - Surface tension liquid-gas, N/m (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Tetrahydrofuran (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
0.0537 298.15 0.0004
0.0537 313.15 0.0004
0.1037 298.15 0.0004
0.1037 313.15 0.0004
0.2081 298.15 0.0004
0.2081 313.15 0.0004
0.3079 298.15 0.0004
0.3079 313.15 0.0004
0.4100 298.15 0.0004
0.4100 313.15 0.0004
0.5085 298.15 0.0004
0.5085 313.15 0.0004
0.5964 298.15 0.0004
0.5964 313.15 0.0004
0.7050 298.15 0.0005
0.7050 313.15 0.0004
0.8051 298.15 0.0005
0.8051 313.15 0.0004
0.8989 298.15 0.0005
0.8989 313.15 0.0004
0.9510 298.15 0.0005
0.9510 313.15 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Tetrahydrofuran (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
0.0537 298.15 0.0004
0.0537 313.15 0.0004
0.1037 298.15 0.0004
0.1037 313.15 0.0004
0.2081 298.15 0.0004
0.2081 313.15 0.0004
0.3079 298.15 0.0004
0.3079 313.15 0.0004
0.4100 298.15 0.0004
0.4100 313.15 0.0004
0.5085 298.15 0.0004
0.5085 313.15 0.0004
0.5964 298.15 0.0004
0.5964 313.15 0.0004
0.7050 298.15 0.0005
0.7050 313.15 0.0004
0.8051 298.15 0.0005
0.8051 313.15 0.0004
0.8989 298.15 0.0005
0.8989 313.15 0.0004
0.9510 298.15 0.0005
0.9510 313.15 0.0004

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0571 871.87
298.15 0.1071 872.53
298.15 0.1884 873.57
298.15 0.2881 874.78
298.15 0.4158 876.28
298.15 0.4933 877.18
298.15 0.6022 878.39
298.15 0.7032 879.48
298.15 0.8064 880.49
298.15 0.8983 881.3
298.15 0.9538 881.69
313.15 0.0562 854.45
313.15 0.1267 855.53
313.15 0.2163 856.77
313.15 0.3482 858.48
313.15 0.4419 859.64
313.15 0.5439 860.87
313.15 0.6661 862.25
313.15 0.7494 863.13
313.15 0.8325 863.96
313.15 0.9104 864.68
313.15 0.9613 865.08

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0571 871.87
298.15 0.1071 872.53
298.15 0.1884 873.57
298.15 0.2881 874.78
298.15 0.4158 876.28
298.15 0.4933 877.18
298.15 0.6022 878.39
298.15 0.7032 879.48
298.15 0.8064 880.49
298.15 0.8983 881.3
298.15 0.9538 881.69
313.15 0.0562 854.45
313.15 0.1267 855.53
313.15 0.2163 856.77
313.15 0.3482 858.48
313.15 0.4419 859.64
313.15 0.5439 860.87
313.15 0.6661 862.25
313.15 0.7494 863.13
313.15 0.8325 863.96
313.15 0.9104 864.68
313.15 0.9613 865.08

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

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0652 0.0222
298.15 0.1201 0.0225
298.15 0.2392 0.0231
298.15 0.3613 0.0235
298.15 0.4622 0.0239
298.15 0.5682 0.0244
298.15 0.6614 0.0249
298.15 0.7586 0.0254
298.15 0.8408 0.0259
298.15 0.9257 0.0265
298.15 0.9662 0.0267
313.15 0.0619 0.0198
313.15 0.1268 0.0203
313.15 0.2531 0.0210
313.15 0.3590 0.0215
313.15 0.4722 0.0221
313.15 0.5669 0.0225
313.15 0.6590 0.0230
313.15 0.7539 0.0234
313.15 0.8338 0.0239
313.15 0.9198 0.0244
313.15 0.9751 0.0248

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

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0652 0.0222
298.15 0.1201 0.0225
298.15 0.2392 0.0231
298.15 0.3613 0.0235
298.15 0.4622 0.0239
298.15 0.5682 0.0244
298.15 0.6614 0.0249
298.15 0.7586 0.0254
298.15 0.8408 0.0259
298.15 0.9257 0.0265
298.15 0.9662 0.0267
313.15 0.0619 0.0198
313.15 0.1268 0.0203
313.15 0.2531 0.0210
313.15 0.3590 0.0215
313.15 0.4722 0.0221
313.15 0.5669 0.0225
313.15 0.6590 0.0230
313.15 0.7539 0.0234
313.15 0.8338 0.0239
313.15 0.9198 0.0244
313.15 0.9751 0.0248

Sources