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 1953
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 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] |
| 353.95 |
0.05000 |
0.90000 |
0.07000 |
0.85000 |
| 353.25 |
0.05700 |
0.37900 |
0.13400 |
0.50200 |
| 353.85 |
0.07000 |
0.85000 |
0.09500 |
0.82000 |
| 352.45 |
0.07600 |
0.59400 |
0.12100 |
0.58400 |
| 353.15 |
0.07800 |
0.83400 |
0.13700 |
0.74900 |
| 352.85 |
0.08200 |
0.48300 |
0.12100 |
0.53500 |
| 353.05 |
0.08400 |
0.42800 |
0.14000 |
0.50700 |
| 354.15 |
0.08500 |
0.17000 |
0.18000 |
0.40000 |
| 352.95 |
0.08700 |
0.51500 |
0.15600 |
0.52100 |
| 352.85 |
0.09100 |
0.49000 |
0.15000 |
0.52800 |
| 352.35 |
0.09200 |
0.73000 |
0.15000 |
0.65000 |
| 352.45 |
0.09500 |
0.59400 |
0.12600 |
0.58800 |
| 352.25 |
0.09500 |
0.72500 |
0.17500 |
0.65000 |
| 353.75 |
0.10000 |
0.19000 |
0.20500 |
0.38500 |
| 352.75 |
0.10000 |
0.79900 |
0.15700 |
0.71900 |
| 352.15 |
0.12000 |
0.70000 |
0.16500 |
0.64000 |
| 352.35 |
0.14000 |
0.16000 |
0.29800 |
0.32500 |
| 351.25 |
0.15000 |
0.54400 |
0.23700 |
0.49900 |
| 351.65 |
0.17100 |
0.31800 |
0.27200 |
0.39100 |
| 352.65 |
0.17400 |
0.08500 |
0.37700 |
0.24000 |
| 351.35 |
0.17600 |
0.40800 |
0.26400 |
0.42900 |
| 350.95 |
0.18200 |
0.52400 |
0.27600 |
0.47500 |
| 351.75 |
0.18600 |
0.19500 |
0.32400 |
0.31400 |
| 352.25 |
0.19000 |
0.10800 |
0.38400 |
0.24400 |
| 350.85 |
0.19700 |
0.60600 |
0.30600 |
0.50400 |
| 350.35 |
0.24000 |
0.42000 |
0.36000 |
0.39000 |
| 350.15 |
0.24500 |
0.43500 |
0.39500 |
0.37500 |
| 350.05 |
0.27000 |
0.64000 |
0.37000 |
0.52500 |
| 349.85 |
0.29000 |
0.41500 |
0.41000 |
0.36500 |
| 349.25 |
0.31500 |
0.58500 |
0.41500 |
0.47000 |
| 349.05 |
0.32300 |
0.59500 |
0.47200 |
0.44200 |
| 348.35 |
0.35600 |
0.43400 |
0.47800 |
0.35100 |
| 348.25 |
0.35800 |
0.28900 |
0.49800 |
0.27500 |
| 348.45 |
0.36500 |
0.54800 |
0.51100 |
0.40500 |
| 347.75 |
0.38500 |
0.28500 |
0.53700 |
0.25600 |
| 347.85 |
0.38500 |
0.41500 |
0.51600 |
0.32600 |
| 347.75 |
0.38800 |
0.52200 |
0.53700 |
0.36200 |
| 347.65 |
0.39500 |
0.20500 |
0.56000 |
0.20500 |
| 347.15 |
0.40800 |
0.48200 |
0.56200 |
0.33700 |
| 347.35 |
0.41000 |
0.22800 |
0.58200 |
0.20800 |
| 347.35 |
0.41600 |
0.36100 |
0.55600 |
0.28800 |
| 346.95 |
0.44500 |
0.35100 |
0.59200 |
0.26600 |
| 346.65 |
0.46400 |
0.22200 |
0.63900 |
0.17500 |
| 346.45 |
0.48200 |
0.31900 |
0.64100 |
0.23200 |
| 346.35 |
0.50000 |
0.35100 |
0.64500 |
0.25100 |
| 345.95 |
0.50100 |
0.24700 |
0.66000 |
0.19200 |
| 345.65 |
0.54000 |
0.21500 |
0.70500 |
0.16000 |
| 345.25 |
0.56200 |
0.30900 |
0.70100 |
0.20800 |
| 345.15 |
0.57000 |
0.21500 |
0.72700 |
0.15600 |
| 344.75 |
0.61500 |
0.17500 |
0.75000 |
0.14000 |
| 344.45 |
0.63000 |
0.18000 |
0.78000 |
0.11000 |
| 344.35 |
0.64000 |
0.16500 |
0.77000 |
0.13000 |
| 342.25 |
0.76200 |
0.11500 |
0.85200 |
0.08000 |
| 341.75 |
0.79100 |
0.09600 |
0.88900 |
0.06400 |
| 341.25 |
0.81100 |
0.09300 |
0.88800 |
0.06000 |
| 340.25 |
0.88700 |
0.06500 |
0.93600 |
0.03800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ochi K.; Kojima K.: On the Vapor-Liquid Equilibria for ternary System consisting of Alcohols and Water. Kagaku Kogaku 33 (1969) 352-357 |
Vapor-Liquid Equilibrium Data Set 2488
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 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] |
| 362.75 |
0.03200 |
0.01300 |
0.19200 |
0.13100 |
| 361.65 |
0.03400 |
0.02500 |
0.17400 |
0.15900 |
| 359.05 |
0.06900 |
0.02500 |
0.22700 |
0.17100 |
| 356.05 |
0.12200 |
0.03900 |
0.35300 |
0.15600 |
| 356.35 |
0.12700 |
0.02000 |
0.41100 |
0.11400 |
| 351.95 |
0.17800 |
0.33500 |
0.22900 |
0.42100 |
| 351.25 |
0.22500 |
0.25100 |
0.32400 |
0.33800 |
| 351.25 |
0.24600 |
0.13100 |
0.39800 |
0.20200 |
| 350.95 |
0.27600 |
0.14600 |
0.43600 |
0.22800 |
| 350.35 |
0.30300 |
0.03100 |
0.61600 |
0.06000 |
| 350.15 |
0.30400 |
0.19400 |
0.43200 |
0.26000 |
| 348.35 |
0.34500 |
0.06500 |
0.62800 |
0.10600 |
| 349.15 |
0.35100 |
0.19600 |
0.48800 |
0.23900 |
| 348.45 |
0.36300 |
0.53600 |
0.49500 |
0.41300 |
| 348.25 |
0.38200 |
0.19000 |
0.53300 |
0.21300 |
| 348.05 |
0.40900 |
0.09100 |
0.62200 |
0.12500 |
| 347.15 |
0.45400 |
0.08400 |
0.66600 |
0.10300 |
| 346.25 |
0.49800 |
0.15000 |
0.66700 |
0.14400 |
| 345.95 |
0.49900 |
0.36400 |
0.64100 |
0.26300 |
| 346.05 |
0.50800 |
0.13700 |
0.68200 |
0.12700 |
| 344.65 |
0.60000 |
0.09600 |
0.75900 |
0.07800 |
| 344.25 |
0.60800 |
0.12000 |
0.77600 |
0.08700 |
| 343.85 |
0.62600 |
0.13700 |
0.78000 |
0.10200 |
| 343.45 |
0.65200 |
0.12700 |
0.80100 |
0.09000 |
| 342.15 |
0.73700 |
0.09100 |
0.84600 |
0.07000 |
| 341.75 |
0.74300 |
0.19100 |
0.85700 |
0.11000 |
| 340.55 |
0.81200 |
0.14300 |
0.89200 |
0.08700 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kohoutova J.; Suska J.; Novak J.P.; Pick J.: Liquid-Vapor Equilibrium XLV. System Methanol-2-Propanol Water. Collect.Czech.Chem.Commun. 35 (1970) 3210-3222 |
Vapor-Liquid Equilibrium Data Set 2522
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 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] |
| 353.35 |
0.08600 |
0.14100 |
0.19800 |
0.40200 |
| 351.45 |
0.10000 |
0.31500 |
0.17800 |
0.46200 |
| 350.95 |
0.11300 |
0.51500 |
0.19900 |
0.48900 |
| 353.35 |
0.13200 |
0.07300 |
0.27000 |
0.39100 |
| 353.35 |
0.14300 |
0.05400 |
0.39600 |
0.21500 |
| 350.75 |
0.17000 |
0.20500 |
0.32600 |
0.34000 |
| 352.75 |
0.17500 |
0.05800 |
0.43100 |
0.20500 |
| 351.05 |
0.19400 |
0.07100 |
0.44200 |
0.20800 |
| 352.15 |
0.19400 |
0.14800 |
0.38600 |
0.28500 |
| 350.75 |
0.20800 |
0.09100 |
0.44400 |
0.22100 |
| 350.95 |
0.23000 |
0.09000 |
0.47000 |
0.19900 |
| 349.65 |
0.24800 |
0.15400 |
0.43800 |
0.25000 |
| 348.05 |
0.30800 |
0.17900 |
0.52600 |
0.22300 |
| 346.85 |
0.41900 |
0.13400 |
0.62500 |
0.16200 |
| 345.95 |
0.44200 |
0.13000 |
0.63400 |
0.14900 |
| 344.75 |
0.54700 |
0.10300 |
0.74800 |
0.09800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Chu J.-C.; Wang S.L.; Levy S.I.; Paul R.: Vapor-Liquid Equilibrium Data. Monograph (1956) 1-754 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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