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 1802
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 345.95 |
0.01880 |
0.37780 |
0.09120 |
0.64500 |
| 340.65 |
0.02530 |
0.67220 |
0.07730 |
0.78690 |
| 342.35 |
0.03310 |
0.55640 |
0.09530 |
0.71910 |
| 337.35 |
0.04290 |
0.87100 |
0.09450 |
0.87100 |
| 337.55 |
0.04490 |
0.84390 |
0.10180 |
0.84960 |
| 343.15 |
0.06280 |
0.30420 |
0.27310 |
0.44200 |
| 345.95 |
0.06390 |
0.11660 |
0.43830 |
0.26900 |
| 340.65 |
0.07240 |
0.49850 |
0.21760 |
0.61390 |
| 337.85 |
0.07570 |
0.71500 |
0.18300 |
0.72300 |
| 342.85 |
0.08400 |
0.04010 |
0.60370 |
0.08580 |
| 340.75 |
0.09050 |
0.39400 |
0.30420 |
0.49550 |
| 342.85 |
0.09100 |
0.18280 |
0.41540 |
0.32800 |
| 341.75 |
0.09520 |
0.26680 |
0.38170 |
0.37460 |
| 337.55 |
0.09710 |
0.62710 |
0.23520 |
0.66150 |
| 335.65 |
0.11200 |
0.75800 |
0.23120 |
0.71800 |
| 338.75 |
0.13140 |
0.37290 |
0.36330 |
0.45650 |
| 338.25 |
0.15150 |
0.40500 |
0.38270 |
0.44000 |
| 338.75 |
0.16650 |
0.23950 |
0.47710 |
0.29040 |
| 334.25 |
0.16960 |
0.70260 |
0.29600 |
0.64070 |
| 337.85 |
0.16970 |
0.37760 |
0.42260 |
0.41260 |
| 337.05 |
0.17580 |
0.44120 |
0.39550 |
0.45430 |
| 337.05 |
0.19540 |
0.34760 |
0.41900 |
0.39700 |
| 337.35 |
0.21910 |
0.19540 |
0.57420 |
0.22060 |
| 333.45 |
0.22380 |
0.64970 |
0.38000 |
0.56940 |
| 336.75 |
0.23650 |
0.07950 |
0.69200 |
0.10550 |
| 334.05 |
0.27080 |
0.49740 |
0.45740 |
0.45050 |
| 335.95 |
0.27120 |
0.23950 |
0.58130 |
0.24820 |
| 333.75 |
0.27120 |
0.51150 |
0.46120 |
0.45000 |
| 334.65 |
0.29500 |
0.34750 |
0.52100 |
0.35430 |
| 333.45 |
0.31550 |
0.48650 |
0.48650 |
0.42650 |
| 334.85 |
0.33140 |
0.29560 |
0.56140 |
0.25630 |
| 335.25 |
0.33300 |
0.13830 |
0.70070 |
0.14610 |
| 331.85 |
0.33430 |
0.54750 |
0.50000 |
0.45500 |
| 331.75 |
0.35100 |
0.49050 |
0.49350 |
0.47000 |
| 330.65 |
0.38420 |
0.57930 |
0.49720 |
0.48710 |
| 333.75 |
0.38750 |
0.30730 |
0.59520 |
0.27950 |
| 334.05 |
0.40850 |
0.11340 |
0.71500 |
0.10390 |
| 332.95 |
0.42420 |
0.26150 |
0.64470 |
0.21450 |
| 334.25 |
0.43150 |
0.09400 |
0.74370 |
0.09660 |
| 329.65 |
0.47150 |
0.47450 |
0.57260 |
0.40500 |
| 333.15 |
0.47220 |
0.10430 |
0.73660 |
0.10880 |
| 332.65 |
0.47780 |
0.15720 |
0.72390 |
0.11850 |
| 332.55 |
0.52900 |
0.08650 |
0.79100 |
0.06050 |
| 329.65 |
0.55900 |
0.38070 |
0.63340 |
0.33960 |
| 331.25 |
0.57020 |
0.20350 |
0.72110 |
0.16870 |
| 330.65 |
0.61400 |
0.20020 |
0.73150 |
0.17700 |
| 330.95 |
0.62090 |
0.16330 |
0.75450 |
0.13880 |
| 330.75 |
0.67500 |
0.10250 |
0.78650 |
0.10800 |
| 329.15 |
0.74440 |
0.18800 |
0.78320 |
0.18050 |
| 329.25 |
0.75290 |
0.17080 |
0.78520 |
0.17640 |
| 329.65 |
0.81000 |
0.08710 |
0.83700 |
0.09330 |
| 330.15 |
0.82200 |
0.04060 |
0.86860 |
0.06330 |
| 329.35 |
0.85360 |
0.04970 |
0.88460 |
0.05690 |
| 329.65 |
0.89930 |
0.03700 |
0.93910 |
0.04340 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Chu J.C.; Getty R.J.; Brennecke L.F.; Paul R.: Distillation Equilibrium Data. Monograph (1950) 1-304 |
Vapor-Liquid Equilibrium Data Set 1803
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 343.15 |
0.10000 |
0.10000 |
0.61000 |
0.13000 |
| 343.15 |
0.10000 |
0.20000 |
0.52000 |
0.24000 |
| 342.55 |
0.10000 |
0.30000 |
0.43000 |
0.35500 |
| 341.95 |
0.10000 |
0.40000 |
0.37000 |
0.45000 |
| 341.15 |
0.10000 |
0.50000 |
0.32000 |
0.54000 |
| 339.65 |
0.10000 |
0.60000 |
0.26000 |
0.63000 |
| 338.15 |
0.10000 |
0.70000 |
0.22000 |
0.71000 |
| 336.65 |
0.10000 |
0.80000 |
0.18500 |
0.78000 |
| 338.15 |
0.20000 |
0.10000 |
0.72000 |
0.07000 |
| 338.65 |
0.20000 |
0.20000 |
0.63500 |
0.18000 |
| 338.65 |
0.20000 |
0.30000 |
0.56000 |
0.28000 |
| 337.65 |
0.20000 |
0.40000 |
0.50000 |
0.37000 |
| 336.65 |
0.20000 |
0.50000 |
0.44000 |
0.47000 |
| 335.65 |
0.20000 |
0.60000 |
0.38500 |
0.55000 |
| 334.15 |
0.20000 |
0.70000 |
0.34000 |
0.62500 |
| 335.95 |
0.30000 |
0.10000 |
0.76000 |
0.06500 |
| 335.85 |
0.30000 |
0.20000 |
0.70000 |
0.15000 |
| 335.45 |
0.30000 |
0.30000 |
0.62500 |
0.25500 |
| 334.65 |
0.30000 |
0.40000 |
0.57000 |
0.34500 |
| 333.65 |
0.30000 |
0.50000 |
0.52000 |
0.41500 |
| 332.65 |
0.30000 |
0.60000 |
0.46500 |
0.50000 |
| 334.65 |
0.40000 |
0.10000 |
0.79000 |
0.06000 |
| 333.95 |
0.40000 |
0.20000 |
0.72500 |
0.15500 |
| 333.15 |
0.40000 |
0.30000 |
0.67000 |
0.24200 |
| 332.55 |
0.40000 |
0.40000 |
0.61500 |
0.32200 |
| 331.55 |
0.40000 |
0.50000 |
0.56500 |
0.40200 |
| 333.15 |
0.50000 |
0.10000 |
0.81000 |
0.06500 |
| 332.55 |
0.50000 |
0.20000 |
0.75000 |
0.16000 |
| 331.75 |
0.50000 |
0.30000 |
0.70000 |
0.23200 |
| 330.75 |
0.50000 |
0.40000 |
0.65000 |
0.31700 |
| 332.25 |
0.60000 |
0.10000 |
0.82000 |
0.08000 |
| 331.45 |
0.60000 |
0.20000 |
0.77000 |
0.16300 |
| 330.45 |
0.60000 |
0.30000 |
0.72000 |
0.24500 |
| 331.35 |
0.70000 |
0.10000 |
0.82700 |
0.09500 |
| 330.35 |
0.70000 |
0.20000 |
0.77800 |
0.18400 |
| 330.35 |
0.80000 |
0.10000 |
0.86000 |
0.10000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Griswold J.; Buford C.B.: Separation of synthesis mixtures Vapor-liquid equilibria of acetone-methanol-water. Ind.Eng.Chem. 41 (1949) 2347-2351 |
Vapor-Liquid Equilibrium Data Set 3735
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 337.90 |
0.20000 |
0.20000 |
0.22900 |
0.59700 |
| 337.21 |
0.40000 |
0.20000 |
0.41400 |
0.45400 |
| 335.20 |
0.60000 |
0.20000 |
0.55700 |
0.37100 |
| 333.67 |
0.20000 |
0.40000 |
0.19100 |
0.68200 |
| 332.33 |
0.40000 |
0.40000 |
0.34800 |
0.58000 |
| 331.00 |
0.20000 |
0.60000 |
0.18400 |
0.73500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Verhoeye L.A.; de Schepper H.: The Vapor-Liquid Equilibria of the Binary, Ternary and Quaternary Systems Formed by Acetone, Methanol Propan-2-ol and Water. J.Appl.Chem.Biotechnol. 23 (1973) 607-619 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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