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 2547
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 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] |
| 378.15 |
0.00500 |
0.54900 |
0.11000 |
0.59300 |
| 377.15 |
0.01000 |
0.47600 |
0.05400 |
0.57400 |
| 376.15 |
0.00800 |
0.23400 |
0.07400 |
0.51400 |
| 370.15 |
0.01700 |
0.47600 |
0.11600 |
0.56700 |
| 369.15 |
0.01700 |
0.83700 |
0.07700 |
0.80300 |
| 362.15 |
0.00900 |
0.27300 |
0.15300 |
0.39200 |
| 356.15 |
0.06000 |
0.68900 |
0.34500 |
0.49100 |
| 355.15 |
0.04800 |
0.51500 |
0.30600 |
0.48300 |
| 355.15 |
0.06900 |
0.79800 |
0.33800 |
0.49000 |
| 353.15 |
0.07400 |
0.61300 |
0.42400 |
0.42600 |
| 351.15 |
0.03100 |
0.46700 |
0.28400 |
0.47000 |
| 351.15 |
0.03900 |
0.50900 |
0.21600 |
0.47700 |
| 348.15 |
0.04100 |
0.79100 |
0.28200 |
0.58200 |
| 348.15 |
0.10300 |
0.57300 |
0.47900 |
0.36500 |
| 347.15 |
0.00900 |
0.15800 |
0.29600 |
0.37200 |
| 347.15 |
0.11800 |
0.55600 |
0.50400 |
0.29600 |
| 347.15 |
0.12100 |
0.44500 |
0.60300 |
0.27400 |
| 346.15 |
0.02300 |
0.25500 |
0.45600 |
0.30600 |
| 346.15 |
0.13900 |
0.44000 |
0.61400 |
0.26000 |
| 345.15 |
0.00500 |
0.14900 |
0.30300 |
0.36500 |
| 345.15 |
0.17300 |
0.42400 |
0.66400 |
0.24300 |
| 345.15 |
0.23100 |
0.47000 |
0.67900 |
0.23100 |
| 345.15 |
0.24200 |
0.38200 |
0.69400 |
0.20900 |
| 344.15 |
0.01600 |
0.08700 |
0.46800 |
0.30400 |
| 344.15 |
0.02300 |
0.16600 |
0.67200 |
0.30700 |
| 344.15 |
0.03000 |
0.41200 |
0.27000 |
0.47000 |
| 344.15 |
0.27000 |
0.47700 |
0.69300 |
0.22600 |
| 343.15 |
0.01300 |
0.17600 |
0.38000 |
0.30600 |
| 343.15 |
0.02300 |
0.30700 |
0.38800 |
0.38700 |
| 343.15 |
0.22300 |
0.40400 |
0.67200 |
0.22500 |
| 343.15 |
0.36800 |
0.44700 |
0.73300 |
0.20300 |
| 342.15 |
0.11200 |
0.35500 |
0.64400 |
0.26700 |
| 342.15 |
0.18500 |
0.45400 |
0.67600 |
0.24000 |
| 341.15 |
0.16700 |
0.58300 |
0.57100 |
0.35600 |
| 341.15 |
0.32000 |
0.50700 |
0.70200 |
0.21700 |
| 339.15 |
0.00600 |
0.08500 |
0.64400 |
0.29200 |
| 339.15 |
0.00800 |
0.08100 |
0.64300 |
0.32200 |
| 336.15 |
0.85700 |
0.13500 |
0.94100 |
0.05400 |
| 335.15 |
0.22700 |
0.18800 |
0.77200 |
0.16600 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Moeller W.P.; Englund S.W.; Tsui T.K.; Othmer D.F.: Compositions of Vapors from Boiling Solutions. Ind.Eng.Chem. 43 (1951) 711-717 |
Vapor-Liquid Equilibrium Data Set 2548
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 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] |
| 397.15 |
0.00900 |
0.49300 |
0.02300 |
0.59600 |
| 393.15 |
0.00400 |
0.11500 |
0.11100 |
0.33600 |
| 390.15 |
0.02800 |
0.54600 |
0.12400 |
0.59700 |
| 389.15 |
0.02700 |
0.83300 |
0.12200 |
0.73700 |
| 388.15 |
0.04000 |
0.82200 |
0.17800 |
0.69600 |
| 384.15 |
0.08400 |
0.77800 |
0.33700 |
0.59200 |
| 382.15 |
0.06200 |
0.56000 |
0.31100 |
0.48200 |
| 381.15 |
0.06300 |
0.69800 |
0.24500 |
0.57000 |
| 381.15 |
0.07400 |
0.72100 |
0.27200 |
0.57500 |
| 381.15 |
0.08700 |
0.66400 |
0.30600 |
0.48000 |
| 379.15 |
0.00900 |
0.52100 |
0.03200 |
0.63000 |
| 377.15 |
0.01000 |
0.47600 |
0.05400 |
0.57400 |
| 377.15 |
0.06900 |
0.51700 |
0.33800 |
0.43100 |
| 376.15 |
0.01400 |
0.22300 |
0.33900 |
0.37800 |
| 376.15 |
0.04700 |
0.44500 |
0.31000 |
0.43800 |
| 376.15 |
0.13000 |
0.64200 |
0.38600 |
0.42700 |
| 375.15 |
0.01500 |
0.58100 |
0.06300 |
0.64500 |
| 372.15 |
0.11400 |
0.48200 |
0.43600 |
0.37000 |
| 371.15 |
0.05100 |
0.35400 |
0.37600 |
0.36900 |
| 371.15 |
0.07100 |
0.40600 |
0.39300 |
0.40400 |
| 371.15 |
0.23800 |
0.57400 |
0.51900 |
0.36600 |
| 370.15 |
0.11300 |
0.48900 |
0.46300 |
0.38800 |
| 369.15 |
0.00400 |
0.12800 |
0.07100 |
0.42800 |
| 369.15 |
0.00700 |
0.08300 |
0.08500 |
0.26900 |
| 367.15 |
0.25000 |
0.42900 |
0.54600 |
0.25300 |
| 364.15 |
0.30900 |
0.45800 |
0.61000 |
0.25800 |
| 364.15 |
0.57400 |
0.31900 |
0.73700 |
0.15600 |
| 362.15 |
0.44600 |
0.26400 |
0.71800 |
0.15100 |
| 362.15 |
0.70900 |
0.23800 |
0.82800 |
0.10100 |
| 361.15 |
0.49300 |
0.24100 |
0.72400 |
0.15300 |
| 361.15 |
0.72100 |
0.22500 |
0.84400 |
0.11000 |
| 361.15 |
0.85700 |
0.09700 |
0.93600 |
0.04400 |
| 361.15 |
0.86300 |
0.11800 |
0.94100 |
0.03900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Moeller W.P.; Englund S.W.; Tsui T.K.; Othmer D.F.: Compositions of Vapors from Boiling Solutions. Ind.Eng.Chem. 43 (1951) 711-717 |
Vapor-Liquid Equilibrium Data Set 2549
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 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] |
| 430.15 |
0.00300 |
0.03300 |
0.00500 |
0.20400 |
| 416.15 |
0.00700 |
0.50000 |
0.02300 |
0.59600 |
| 416.15 |
0.07400 |
0.88900 |
0.13600 |
0.83900 |
| 415.15 |
0.01000 |
0.54300 |
0.04200 |
0.62700 |
| 412.15 |
0.00700 |
0.21100 |
0.15600 |
0.48700 |
| 412.15 |
0.02100 |
0.52800 |
0.08600 |
0.55200 |
| 411.15 |
0.01300 |
0.83300 |
0.03700 |
0.83000 |
| 411.15 |
0.05800 |
0.66800 |
0.16600 |
0.59900 |
| 410.15 |
0.01300 |
0.88200 |
0.02500 |
0.87000 |
| 409.15 |
0.02800 |
0.72500 |
0.06700 |
0.73300 |
| 408.15 |
0.03600 |
0.73000 |
0.09300 |
0.69400 |
| 407.15 |
0.02000 |
0.65500 |
0.05400 |
0.68400 |
| 405.15 |
0.01200 |
0.78400 |
0.01300 |
0.81000 |
| 402.15 |
0.02000 |
0.29200 |
0.21700 |
0.50700 |
| 401.15 |
0.00600 |
0.16400 |
0.11600 |
0.42800 |
| 398.15 |
0.04800 |
0.54700 |
0.18600 |
0.55300 |
| 397.15 |
0.06800 |
0.81700 |
0.20800 |
0.69400 |
| 396.15 |
0.13000 |
0.72500 |
0.28600 |
0.56400 |
| 395.15 |
0.04000 |
0.34600 |
0.39800 |
0.44900 |
| 394.15 |
0.00300 |
0.08700 |
0.30800 |
0.30500 |
| 392.15 |
0.03300 |
0.44100 |
0.25500 |
0.49000 |
| 386.15 |
0.18700 |
0.58200 |
0.38500 |
0.41700 |
| 383.15 |
0.11300 |
0.25700 |
0.55900 |
0.31600 |
| 379.15 |
0.66900 |
0.29500 |
0.80000 |
0.17000 |
| 377.15 |
0.51900 |
0.25000 |
0.72300 |
0.16400 |
| 376.15 |
0.53200 |
0.42100 |
0.74200 |
0.25100 |
| 376.15 |
0.89200 |
0.05000 |
0.91500 |
0.05400 |
| 375.15 |
0.76600 |
0.08700 |
0.79900 |
0.06200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Moeller W.P.; Englund S.W.; Tsui T.K.; Othmer D.F.: Compositions of Vapors from Boiling Solutions. Ind.Eng.Chem. 43 (1951) 711-717 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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