Mixture of Ethanol, 2,2,2-trifluoro- + Toluene

Excel

Ethanol, 2,2,2-trifluoro-

Name
Ethanol, 2,2,2-trifluoro-
InChI
InChI=1S/C2H3F3O/c3-2(4,5)1-6/h6H,1H2
InChI Key
RHQDFWAXVIIEBN-UHFFFAOYSA-N
Formula
C2H3F3O
SMILES
OCC(F)(F)F
Mol. Weight (g/mol)
100.04
CAS
75-89-8

Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3
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. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Toluene (2) [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Mole fraction of Toluene (2) - Liquid Mole fraction of Toluene (2) - Gas
0.0230 0.0590
0.0670 0.1300
0.1120 0.1740
0.1900 0.2000
0.4600 0.2490
0.5710 0.2660
0.6730 0.2760
0.8210 0.2810
0.8790 0.3310
0.8870 0.3480
0.9270 0.4170
0.9610 0.5410
0.9760 0.6530

Mole fraction of Toluene (2) [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Mole fraction of Toluene (2) - Liquid Mole fraction of Toluene (2) - Gas
0.0230 0.0590
0.0670 0.1300
0.1120 0.1740
0.1900 0.2000
0.4600 0.2490
0.5710 0.2660
0.6730 0.2760
0.8210 0.2810
0.8790 0.3310
0.8870 0.3480
0.9270 0.4170
0.9610 0.5410
0.9760 0.6530

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Mole fraction of Toluene (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0230 346.50
0.0670 345.60
0.1120 345.20
0.1900 345.50
0.4600 345.80
0.5710 346.20
0.6730 346.80
0.8210 347.80
0.8790 351.90
0.8870 352.60
0.9270 356.50
0.9610 362.90
0.9760 370.40

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Mole fraction of Toluene (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0230 346.50
0.0670 345.60
0.1120 345.20
0.1900 345.50
0.4600 345.80
0.5710 346.20
0.6730 346.80
0.8210 347.80
0.8790 351.90
0.8870 352.60
0.9270 356.50
0.9610 362.90
0.9760 370.40

Sources