Mixture of Trichloromethane + Isopropyl Alcohol

Excel

Trichloromethane

Name
Trichloromethane
InChI
InChI=1S/CHCl3/c2-1(3)4/h1H
InChI Key
HEDRZPFGACZZDS-UHFFFAOYSA-N
Formula
CHCl3
SMILES
ClC(Cl)Cl
Mol. Weight (g/mol)
119.38
CAS
67-66-3

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)
  3. Vapor Liquid Equilibrium at Constant Pressure (2)
  4. Vapor Liquid Equilibrium at Constant Temperature

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Trichloromethane (1) - Liquid Mole fraction of Trichloromethane (1) - Gas
0.0760 0.2100
0.1760 0.4040
0.2680 0.5250
0.3420 0.6050
0.4340 0.6760
0.5340 0.7390
0.6450 0.7870
0.7950 0.8540
0.8980 0.9110
0.9480 0.9490

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Trichloromethane (1) - Liquid Mole fraction of Trichloromethane (1) - Gas
0.0760 0.2100
0.1760 0.4040
0.2680 0.5250
0.3420 0.6050
0.4340 0.6760
0.5340 0.7390
0.6450 0.7870
0.7950 0.8540
0.8980 0.9110
0.9480 0.9490

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Trichloromethane (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0760 351.05
0.1760 346.75
0.2680 343.95
0.3420 340.95
0.4340 338.85
0.5340 337.25
0.6450 335.85
0.7950 334.75
0.8980 334.35
0.9480 334.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Trichloromethane (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0760 351.05
0.1760 346.75
0.2680 343.95
0.3420 340.95
0.4340 338.85
0.5340 337.25
0.6450 335.85
0.7950 334.75
0.8980 334.35
0.9480 334.25

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Trichloromethane (1) - Liquid y1[mol/mol] of Trichloromethane (1) - Vapour
355.55 0.0000 0.0000
354.15 0.0300 0.0910
353.15 0.0520 0.1300
351.65 0.0910 0.2170
348.85 0.1350 0.3340
347.15 0.1920 0.4200
345.75 0.2320 0.4850
343.95 0.3100 0.5710
341.65 0.3900 0.6500
340.35 0.4550 0.7100
339.25 0.5050 0.7450
338.65 0.5500 0.7550
337.75 0.6100 0.7800
336.65 0.6850 0.8110
335.95 0.7300 0.8300
335.15 0.7900 0.8500
334.85 0.8150 0.8650
334.35 0.8700 0.8900
333.95 0.9210 0.9210
334.05 0.9800 0.9600
334.25 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Trichloromethane (1) - Liquid y1[mol/mol] of Trichloromethane (1) - Vapour
353.65 0.0350 0.0890
352.05 0.0690 0.1670
350.85 0.0920 0.2220
349.15 0.1320 0.3040
347.15 0.1800 0.3930
346.15 0.2040 0.4320
345.15 0.2330 0.4720
343.35 0.2920 0.5440
341.75 0.3460 0.6000
341.05 0.3680 0.6210
339.75 0.4290 0.6680
338.05 0.5130 0.7240
336.55 0.6300 0.7820
336.35 0.6450 0.7890
335.35 0.7500 0.8370
334.85 0.8220 0.8700
334.45 0.9080 0.9190
334.45 0.9380 0.9400
334.25 0.9550 0.9540
334.25 0.9770 0.9750

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 323.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Trichloromethane (1) - Liquid y1[mol/mol] of Trichloromethane (1) - Vapour
33.077 0.0990 0.3420
39.757 0.1760 0.4920
47.263 0.2870 0.6170
52.756 0.3800 0.6940
57.889 0.4890 0.7570
61.248 0.5890 0.8010
62.395 0.6230 0.8120
66.288 0.7700 0.8650
67.861 0.8360 0.8950
68.874 0.9390 0.9470
69.088 0.9530 0.9570

Sources