aceton scetic acid eq -data

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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 theDortmund Data Bank . For more data or any further information please search the DDB or contact DDBST . Vapor-Liquid Equilibrium Data Set 202 Components No. Formula Molar Mass CAS Registry Number Name 1 C 3 H 6 O 58.080 67-64-1 Acetone 2 C 2 H 4 O 2 60.053 64-19-7 Acetic acid Constant Value Pressure 101.33 kPa Data Table T [K] x 1 [mol/mol] y 1 [mol/mol] 391.25 0.00000 0.00000 383.15 0.05000 0.16200 376.95 0.10000 0.30600 366.25 0.20000 0.55700 358.95 0.30000 0.72500 352.85 0.40000 0.84000 347.75 0.50000 0.91200 343.35 0.60000 0.94700 339.25 0.70000 0.96900 335.75 0.80000 0.98400 332.35 0.90000 0.99300 329.25 1.00000 1.00000 (T - temperature, x - liquid mole fraction, y - vapor mole fraction) Reference

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Page 1: Aceton Scetic Acid Eq -Data

Vapor-Liquid Equilibrium DataThe 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 theDortmund

Data Bank. For more data or any further information please search the DDB or contact DDBST.

Vapor-Liquid Equilibrium Data Set 202

Components

No. Formula Molar Mass CAS Registry Number Name

1 C3H6O 58.080 67-64-1 Acetone

2 C2H4O2 60.053 64-19-7 Acetic acid

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]

391.25 0.00000 0.00000

383.15 0.05000 0.16200

376.95 0.10000 0.30600

366.25 0.20000 0.55700

358.95 0.30000 0.72500

352.85 0.40000 0.84000

347.75 0.50000 0.91200

343.35 0.60000 0.94700

339.25 0.70000 0.96900

335.75 0.80000 0.98400

332.35 0.90000 0.99300

329.25 1.00000 1.00000

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

Reference

Source

Othmer D.F.: Composition of Vapors from Boiling Binary Solutions. Ind.Eng.Chem. 35 (1943) 614-620

Page 2: Aceton Scetic Acid Eq -Data

Vapor-Liquid Equilibrium Data Set 268

Components

No. Formula Molar Mass CAS Registry Number Name

1 C3H6O 58.080 67-64-1 Acetone

2 C2H4O2 60.053 64-19-7 Acetic acid

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]

385.25 0.04200 0.10800

380.55 0.10300 0.25700

379.45 0.12000 0.28900

379.25 0.12700 0.31000

378.55 0.11800 0.30300

377.75 0.15800 0.35600

374.55 0.19400 0.43300

371.85 0.18600 0.46400

367.45 0.22600 0.56400

365.65 0.23600 0.58000

363.55 0.27100 0.63000

360.15 0.29400 0.66000

359.45 0.30700 0.70900

351.75 0.43300 0.84400

347.35 0.53800 0.92000

343.95 0.55000 0.91800

338.75 0.66800 0.96600

336.75 0.76100 0.98100

333.85 0.93500 0.99700

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

Reference

Source

Holmes R.C.: Vapor-Liquid Equilibria of the System Acetone-Acetic Acid-Water. Ind.Eng.Chem. Ind.Ed. 34 (1942) 345-350

Page 3: Aceton Scetic Acid Eq -Data

Vapor-Liquid Equilibrium Data Set 3811

Components

No. Formula Molar Mass CAS Registry Number Name

1 C3H6O 58.080 67-64-1 Acetone

2 C2H4O2 60.053 64-19-7 Acetic acid

Constant Value

Temperature 303.15 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]

2.640 0.00000 0.00000

6.906 0.15100 0.65600

11.732 0.29320 0.83020

18.558 0.48130 0.92820

20.692 0.54060 0.94730

23.465 0.61360 0.96560

27.184 0.72420 0.98300

32.464 0.87360 0.99550

36.530 1.00000 1.00000

(P - pressure, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source

Murphy N.F.: A New Correlation for Binary Systems with an Associating Component. Chem.Eng.Sci. 20 (1965) 757-769

Diagrams

Page 4: Aceton Scetic Acid Eq -Data

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List of All References

Source

Holmes R.C.: Vapor-Liquid Equilibria of the System Acetone-Acetic Acid-Water. Ind.Eng.Chem. Ind.Ed. 34 (1942) 345-350

Othmer D.F.: Composition of Vapors from Boiling Binary Solutions. Ind.Eng.Chem. 35 (1943) 614-620

Murphy N.F.: A New Correlation for Binary Systems with an Associating Compone