Mixture of Trichloromethane + Acetic acid + Water

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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

Acetic acid

Name
Acetic acid
InChI
InChI=1S/C2H4O2/c1-2(3)4/h1H3,(H,3,4)
InChI Key
QTBSBXVTEAMEQO-UHFFFAOYSA-N
Formula
C2H4O2
SMILES
CC(=O)O
Mol. Weight (g/mol)
60.05
CAS
64-19-7

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Mole fraction (2)
  2. Vapor Liquid Equilibrium at Constant Pressure (2)

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Acetic acid (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Acetic acid (2) - Liquid mixture 2
0.9989 0.0000 0.0092 0.0000
0.9691 0.0296 0.0286 0.0332
0.9277 0.0707 0.0367 0.0956
0.8792 0.1187 0.0531 0.1711
0.8276 0.1692 0.0770 0.2476
0.7571 0.2381 0.1041 0.3305

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Acetic acid (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Acetic acid (2) - Liquid mixture 2
0.9989 0.0000 0.0092 0.0000
0.9691 0.0296 0.0286 0.0332
0.9277 0.0707 0.0367 0.0956
0.8792 0.1187 0.0531 0.1711
0.8276 0.1692 0.0770 0.2476
0.7571 0.2381 0.1041 0.3305

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetic acid (2) - Liquid x2[mol/mol] of Water (3) - Liquid
351.35 0.3058 0.6752
353.35 0.3096 0.6725
356.65 0.3209 0.6639
359.75 0.3164 0.6710
349.35 0.3538 0.6088
351.85 0.3616 0.6036
356.45 0.3708 0.6048
358.05 0.3699 0.6095
358.25 0.3730 0.6098
339.55 0.3923 0.5146
339.95 0.3966 0.5121
340.15 0.4024 0.5080
340.55 0.4016 0.5116
341.35 0.4036 0.5154
339.95 0.4544 0.4049
340.85 0.4605 0.4049
341.35 0.4624 0.4090
342.05 0.4647 0.4219
342.95 0.4704 0.4203
357.05 0.6935 0.1948
357.75 0.7037 0.1884
358.35 0.7056 0.1930
359.95 0.4792 0.4912
362.45 0.4793 0.4972
364.35 0.4899 0.4918
363.25 0.6767 0.2704
364.25 0.6725 0.2805
365.25 0.6792 0.2773
374.45 0.8490 0.1093
375.35 0.8442 0.1204
376.15 0.8453 0.1229
377.45 0.8451 0.1280
342.95 0.5293 0.2051
342.95 0.5444 0.1886
346.25 0.4864 0.4230
347.85 0.4913 0.4231

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetic acid (2) - Liquid x2[mol/mol] of Water (3) - Liquid y1[mol/mol] of Acetic acid (2) - Vapour y2[mol/mol] of Water (3) - Vapour
329.95 0.0702 0.0043 0.0116 0.8004
329.95 0.0579 0.9048 0.0116 0.8004
330.35 0.1050 0.0058 0.0148 0.7883
330.35 0.1008 0.8867 0.0148 0.7883
330.65 0.1258 0.0075 0.0130 0.7765
330.65 0.0933 0.7881 0.0130 0.7765
331.65 0.1971 0.0179 0.0210 0.7693
331.65 0.1671 0.7140 0.0210 0.7693
332.15 0.2337 0.0283 0.0245 0.7796
332.15 0.2348 0.6842 0.0245 0.7796
332.35 0.2504 0.0340 0.0243 0.7708
332.35 0.2364 0.6221 0.0243 0.7708
333.15 0.3013 0.0739 0.0321 0.7594
332.95 0.3392 0.1352 0.0330 0.7856
332.95 0.3452 0.3966 0.0330 0.7856
332.45 0.2987 0.0595 0.0312 0.7826
332.45 0.3146 0.5586 0.0312 0.7826
333.55 0.2485 0.7071 0.0268 0.8054
340.05 0.5109 0.4558 0.0944 0.7820
350.15 0.6620 0.1539 0.2002 0.6050
367.55 0.6084 0.0239 0.3754 0.2025
354.05 0.4830 0.0409 0.1969 0.4434
370.25 0.6018 0.0150 0.3771 0.2315

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