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

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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

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
0.0557 313.15 0.0004
0.0634 298.15 0.0005
0.0959 313.15 0.0004
0.1288 298.15 0.0005
0.1963 313.15 0.0004
0.2423 298.15 0.0005
0.2960 313.15 0.0004
0.3198 298.15 0.0005
0.3892 313.15 0.0004
0.4555 298.15 0.0005
0.5210 313.15 0.0004
0.5341 298.15 0.0005
0.5951 313.15 0.0004
0.6368 313.15 0.0004
0.6598 298.15 0.0005
0.7441 298.15 0.0005
0.8089 313.15 0.0004
0.8407 298.15 0.0005
0.8916 298.15 0.0005
0.9009 313.15 0.0004
0.9526 313.15 0.0004
0.9610 298.15 0.0005

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
0.0557 313.15 0.0004
0.0634 298.15 0.0005
0.0959 313.15 0.0004
0.1288 298.15 0.0005
0.1963 313.15 0.0004
0.2423 298.15 0.0005
0.2960 313.15 0.0004
0.3198 298.15 0.0005
0.3892 313.15 0.0004
0.4555 298.15 0.0005
0.5210 313.15 0.0004
0.5341 298.15 0.0005
0.5951 313.15 0.0004
0.6368 313.15 0.0004
0.6598 298.15 0.0005
0.7441 298.15 0.0005
0.8089 313.15 0.0004
0.8407 298.15 0.0005
0.8916 298.15 0.0005
0.9009 313.15 0.0004
0.9526 313.15 0.0004
0.9610 298.15 0.0005

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 0.0526 838.96
298.15 0.1013 841.3
298.15 0.1967 845.97
298.15 0.3170 851.56
298.15 0.4131 856.07
298.15 0.5061 860.43
298.15 0.6033 864.82
298.15 0.7087 869.5
298.15 0.8132 874.03
298.15 0.9031 877.92
298.15 0.9545 880.08
313.15 0.0559 821.08
313.15 0.1219 824.43
313.15 0.2311 829.82
313.15 0.3509 835.82
313.15 0.4172 839.02
313.15 0.5110 843.5
313.15 0.5950 847.38
313.15 0.7018 852.4
313.15 0.8044 856.93
313.15 0.9004 861.05
313.15 0.9545 863.37

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 0.0526 838.96
298.15 0.1013 841.3
298.15 0.1967 845.97
298.15 0.3170 851.56
298.15 0.4131 856.07
298.15 0.5061 860.43
298.15 0.6033 864.82
298.15 0.7087 869.5
298.15 0.8132 874.03
298.15 0.9031 877.92
298.15 0.9545 880.08
313.15 0.0559 821.08
313.15 0.1219 824.43
313.15 0.2311 829.82
313.15 0.3509 835.82
313.15 0.4172 839.02
313.15 0.5110 843.5
313.15 0.5950 847.38
313.15 0.7018 852.4
313.15 0.8044 856.93
313.15 0.9004 861.05
313.15 0.9545 863.37

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 0.0664 0.0193
298.15 0.1332 0.0197
298.15 0.2532 0.0205
298.15 0.3652 0.0213
298.15 0.4851 0.0221
298.15 0.5768 0.0228
298.15 0.6804 0.0237
298.15 0.7747 0.0245
298.15 0.8446 0.0252
298.15 0.9372 0.0262
298.15 0.9656 0.0266
313.15 0.0427 0.0170
313.15 0.1236 0.0172
313.15 0.1853 0.0175
313.15 0.2856 0.0182
313.15 0.3852 0.0189
313.15 0.5033 0.0199
313.15 0.6055 0.0208
313.15 0.6963 0.0215
313.15 0.7940 0.0225
313.15 0.8900 0.0235
313.15 0.9446 0.0243

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 0.0664 0.0193
298.15 0.1332 0.0197
298.15 0.2532 0.0205
298.15 0.3652 0.0213
298.15 0.4851 0.0221
298.15 0.5768 0.0228
298.15 0.6804 0.0237
298.15 0.7747 0.0245
298.15 0.8446 0.0252
298.15 0.9372 0.0262
298.15 0.9656 0.0266
313.15 0.0427 0.0170
313.15 0.1236 0.0172
313.15 0.1853 0.0175
313.15 0.2856 0.0182
313.15 0.3852 0.0189
313.15 0.5033 0.0199
313.15 0.6055 0.0208
313.15 0.6963 0.0215
313.15 0.7940 0.0225
313.15 0.8900 0.0235
313.15 0.9446 0.0243

Sources