Dortmund Data Bank

Vapor-Liquid Equilibrium Data

The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.

Vapor-Liquid Equilibrium Data Set 8844

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H4O2 60.053 64-19-7 Acetic acid
2 H2O 18.015 7732-18-5 Water
3 CHCl3 119.377 67-66-3 Chloroform
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] x2 [mol/mol]
351.35 0.30584 0.67521
353.35 0.30957 0.67255
356.65 0.32086 0.66391
359.75 0.31642 0.67102
349.35 0.35375 0.60876
351.85 0.36164 0.60358
356.45 0.37076 0.60475
358.05 0.36993 0.60946
358.25 0.37303 0.60975
339.55 0.39227 0.51459
339.95 0.39662 0.51210
340.15 0.40238 0.50803
340.55 0.40164 0.51161
341.35 0.40356 0.51539
339.95 0.45436 0.40490
340.85 0.46050 0.40488
341.35 0.46240 0.40904
342.05 0.46473 0.42187
342.95 0.47037 0.42034
357.05 0.69353 0.19476
357.75 0.70374 0.18839
358.35 0.70555 0.19298
359.95 0.47918 0.49116
362.45 0.47935 0.49722
364.35 0.48991 0.49179
363.25 0.67667 0.27036
364.25 0.67248 0.28048
365.25 0.67918 0.27726
374.45 0.84896 0.10931
375.35 0.84422 0.12039
376.15 0.84526 0.12288
377.45 0.84512 0.12801
342.95 0.52926 0.20508
342.95 0.54440 0.18858
346.25 0.48637 0.42304
347.85 0.49126 0.42306

(T - temperature, x - liquid mole fraction)

Reference

Source
Campbell A.N.; Gieskes J.M.T.M.: The Isobaric Boiling Points of the System Acetic Acid-Chloroform-Water at a Pressure of 760mmHg. Can.J.Chem. 42 (1964) 186-189


Vapor-Liquid Equilibrium Data Set 12799

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H4O2 60.053 64-19-7 Acetic acid
2 CHCl3 119.377 67-66-3 Chloroform
3 H2O 18.015 7732-18-5 Water
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] x2 [mol/mol] y1 [mol/mol] y2 [mol/mol]
329.95 0.07023 0.004304 0.011615 0.80039
329.95 0.05790 0.90475 0.011615 0.80039
330.35 0.10504 0.005785 0.01477 0.78835
330.35 0.10084 0.88672 0.01477 0.78835
330.65 0.12583 0.007459 0.01296 0.77652
330.65 0.09326 0.78808 0.01296 0.77652
331.65 0.19715 0.017902 0.020974 0.76935
331.65 0.16709 0.71399 0.020974 0.76935
332.15 0.23373 0.02830 0.024497 0.77958
332.15 0.23481 0.68424 0.024497 0.77958
332.35 0.25042 0.03404 0.02427 0.77082
332.35 0.23645 0.62213 0.02427 0.77082
333.15 0.30129 0.07386 0.03209 0.75940
332.95 0.33920 0.13519 0.032986 0.78564
332.95 0.34515 0.39657 0.032986 0.78564
332.45 0.29867 0.05948 0.031216 0.78263
332.45 0.31459 0.55863 0.031216 0.78263
333.55 0.24846 0.70709 0.02685 0.80537
340.05 0.51089 0.45582 0.09442 0.78197
350.15 0.66199 0.15389 0.20021 0.60499
367.55 0.60840 0.023897 0.37544 0.20250
354.05 0.48303 0.04091 0.19692 0.44335
370.25 0.60180 0.015023 0.37715 0.23149

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Conti J.J.; Othmer D.F.; Gilmont R.: Composition of Vapors from Boiling Binary Solutions. Systems Containing Formic Acid, Acetic Acid, Water and Chloroform. J.Chem.Eng.Data 5 (1960) 301-307

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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