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 2553
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 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] |
| 363.15 |
0.00300 |
0.01200 |
0.14000 |
0.17800 |
| 355.15 |
0.00400 |
0.07500 |
0.09700 |
0.40500 |
| 353.15 |
0.00400 |
0.59000 |
0.01500 |
0.61400 |
| 353.15 |
0.00400 |
0.64400 |
0.00900 |
0.66000 |
| 353.15 |
0.00500 |
0.69000 |
0.01500 |
0.68500 |
| 353.15 |
0.00500 |
0.80200 |
0.01500 |
0.77000 |
| 353.15 |
0.00800 |
0.74400 |
0.01900 |
0.71500 |
| 353.15 |
0.00900 |
0.24300 |
0.10200 |
0.46400 |
| 353.15 |
0.00900 |
0.38600 |
0.05300 |
0.53000 |
| 353.15 |
0.00900 |
0.76600 |
0.01500 |
0.74400 |
| 363.15 |
0.01000 |
0.00800 |
0.21200 |
0.10200 |
| 353.15 |
0.01000 |
0.52000 |
0.03000 |
0.59000 |
| 353.15 |
0.01100 |
0.07400 |
0.22400 |
0.32500 |
| 355.15 |
0.01200 |
0.06200 |
0.13800 |
0.37200 |
| 353.15 |
0.01300 |
0.07200 |
0.21800 |
0.33600 |
| 355.15 |
0.01400 |
0.04400 |
0.21800 |
0.29300 |
| 353.15 |
0.01600 |
0.15100 |
0.13500 |
0.43500 |
| 353.15 |
0.01600 |
0.27800 |
0.09000 |
0.48000 |
| 353.15 |
0.01700 |
0.94100 |
0.08800 |
0.85800 |
| 353.15 |
0.01750 |
0.17500 |
0.12200 |
0.44800 |
| 355.15 |
0.01800 |
0.04500 |
0.21400 |
0.29200 |
| 355.15 |
0.02000 |
0.01900 |
0.34900 |
0.15300 |
| 353.15 |
0.02600 |
0.02000 |
0.41000 |
0.14200 |
| 350.15 |
0.03400 |
0.03600 |
0.45200 |
0.16500 |
| 348.15 |
0.04200 |
0.01900 |
0.57700 |
0.07800 |
| 348.15 |
0.04700 |
0.02200 |
0.55100 |
0.10100 |
| 350.15 |
0.04700 |
0.17800 |
0.28600 |
0.34400 |
| 346.15 |
0.05000 |
0.04000 |
0.52500 |
0.14000 |
| 350.15 |
0.05900 |
0.46600 |
0.17600 |
0.47800 |
| 348.15 |
0.06500 |
0.13000 |
0.37700 |
0.26600 |
| 346.15 |
0.07800 |
0.09500 |
0.46000 |
0.21100 |
| 348.15 |
0.08200 |
0.29400 |
0.32800 |
0.34200 |
| 343.15 |
0.08300 |
0.03600 |
0.63200 |
0.08600 |
| 348.15 |
0.09000 |
0.48000 |
0.28400 |
0.42100 |
| 348.15 |
0.10500 |
0.61000 |
0.27000 |
0.49600 |
| 348.15 |
0.10800 |
0.67500 |
0.27300 |
0.53100 |
| 342.15 |
0.11000 |
0.05000 |
0.63800 |
0.10800 |
| 346.15 |
0.12400 |
0.29000 |
0.40000 |
0.29600 |
| 341.15 |
0.13200 |
0.05300 |
0.64200 |
0.10900 |
| 346.15 |
0.14000 |
0.58000 |
0.33800 |
0.45600 |
| 342.15 |
0.14800 |
0.11400 |
0.58900 |
0.15700 |
| 343.15 |
0.15500 |
0.15000 |
0.53000 |
0.19400 |
| 339.15 |
0.16600 |
0.02400 |
0.72800 |
0.04100 |
| 341.15 |
0.19000 |
0.12000 |
0.60000 |
0.15000 |
| 343.15 |
0.19200 |
0.28100 |
0.49200 |
0.25500 |
| 338.15 |
0.19800 |
0.03400 |
0.73100 |
0.04900 |
| 339.15 |
0.20500 |
0.06800 |
0.68000 |
0.09700 |
| 342.15 |
0.21200 |
0.18200 |
0.53700 |
0.21900 |
| 343.15 |
0.22600 |
0.53200 |
0.47700 |
0.35600 |
| 343.15 |
0.22700 |
0.55000 |
0.47400 |
0.36600 |
| 342.15 |
0.23600 |
0.33600 |
0.52000 |
0.25600 |
| 338.15 |
0.24600 |
0.05700 |
0.73700 |
0.03700 |
| 339.15 |
0.25300 |
0.11000 |
0.65200 |
0.12700 |
| 342.15 |
0.26200 |
0.49200 |
0.49700 |
0.33300 |
| 341.15 |
0.26600 |
0.28200 |
0.56000 |
0.22000 |
| 337.15 |
0.26900 |
0.05200 |
0.74700 |
0.04600 |
| 341.15 |
0.29400 |
0.48400 |
0.54500 |
0.30800 |
| 339.15 |
0.32400 |
0.19700 |
0.64000 |
0.16400 |
| 338.15 |
0.34400 |
0.17500 |
0.68700 |
0.11700 |
| 336.15 |
0.35600 |
0.06400 |
0.74500 |
0.05900 |
| 339.15 |
0.37600 |
0.42100 |
0.61600 |
0.25900 |
| 338.15 |
0.38200 |
0.27400 |
0.63900 |
0.18900 |
| 337.15 |
0.38500 |
0.17500 |
0.70200 |
0.11400 |
| 337.15 |
0.38900 |
0.21200 |
0.67400 |
0.15400 |
| 338.15 |
0.39900 |
0.41500 |
0.65700 |
0.22900 |
| 335.15 |
0.41000 |
0.03900 |
0.76600 |
0.05100 |
| 338.15 |
0.41500 |
0.46500 |
0.67300 |
0.25000 |
| 337.15 |
0.43600 |
0.38600 |
0.68300 |
0.21200 |
| 337.15 |
0.43800 |
0.30000 |
0.67900 |
0.17500 |
| 336.15 |
0.44800 |
0.17500 |
0.71600 |
0.12500 |
| 335.15 |
0.45800 |
0.06500 |
0.77000 |
0.06000 |
| 336.15 |
0.46000 |
0.22800 |
0.69800 |
0.14300 |
| 336.15 |
0.46600 |
0.31000 |
0.70500 |
0.17300 |
| 335.15 |
0.50200 |
0.16100 |
0.74600 |
0.09500 |
| 334.15 |
0.52300 |
0.06700 |
0.79900 |
0.04300 |
| 335.15 |
0.52400 |
0.26700 |
0.73100 |
0.15300 |
| 335.15 |
0.55100 |
0.29700 |
0.74000 |
0.16900 |
| 333.15 |
0.56900 |
0.05000 |
0.82600 |
0.02600 |
| 334.15 |
0.58500 |
0.17700 |
0.77800 |
0.10300 |
| 334.15 |
0.62000 |
0.26100 |
0.79500 |
0.14400 |
| 333.15 |
0.62500 |
0.12600 |
0.80000 |
0.07000 |
| 332.15 |
0.65200 |
0.06200 |
0.83700 |
0.03100 |
| 333.15 |
0.67300 |
0.21100 |
0.83800 |
0.10300 |
| 332.15 |
0.69900 |
0.10500 |
0.85500 |
0.04000 |
| 332.15 |
0.73600 |
0.17300 |
0.86000 |
0.09300 |
| 331.15 |
0.75700 |
0.05900 |
0.86500 |
0.03600 |
| 331.15 |
0.80800 |
0.13000 |
0.90100 |
0.05200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Choffé B.; Asselineau L.: Première partie: étude des équilibres binaires. Rev.Inst.Francais Petrol. 11 (1956) 948-954 |
Vapor-Liquid Equilibrium Data Set 3737
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 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] |
| 334.05 |
0.20000 |
0.60000 |
0.10400 |
0.78800 |
| 338.40 |
0.40000 |
0.40000 |
0.22200 |
0.65900 |
| 344.60 |
0.60000 |
0.20000 |
0.41400 |
0.42800 |
| 337.25 |
0.20000 |
0.40000 |
0.11400 |
0.70500 |
| 343.85 |
0.40000 |
0.20000 |
0.29700 |
0.46600 |
| 343.01 |
0.20000 |
0.20000 |
0.20900 |
0.54600 |
(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 |
Vapor-Liquid Equilibrium Data Set 3738
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 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
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 158.770 |
0.31500 |
0.58500 |
0.18370 |
0.73210 |
| 154.650 |
0.29000 |
0.52000 |
0.16580 |
0.70020 |
| 150.270 |
0.24500 |
0.45500 |
0.15310 |
0.67240 |
| 144.811 |
0.21000 |
0.39000 |
0.14310 |
0.65170 |
| 139.561 |
0.17500 |
0.32500 |
0.13760 |
0.63370 |
| 134.870 |
0.14000 |
0.26000 |
0.13660 |
0.61750 |
| 128.200 |
0.10500 |
0.19500 |
0.13610 |
0.59880 |
| 123.321 |
0.07000 |
0.13000 |
0.14630 |
0.57330 |
| 105.710 |
0.03500 |
0.06500 |
0.15110 |
0.50960 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ramalho R.S.; Drolet J.F.: Vapor-Liquid Equilibria Data for the Ternary System Acetone-2-Propanol-Water and Corresponding Binaries from Total Pressure Measurements. J.Chem.Eng.Data 16 (1971) 12-15 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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