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 214
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
24.691 |
0.00000 |
0.00000 |
24.785 |
0.00410 |
0.00980 |
26.238 |
0.02100 |
0.07840 |
29.504 |
0.06420 |
0.20900 |
29.704 |
0.06830 |
0.21680 |
33.011 |
0.11170 |
0.32190 |
36.210 |
0.15840 |
0.40890 |
44.530 |
0.33380 |
0.59510 |
46.823 |
0.38790 |
0.63890 |
51.596 |
0.54300 |
0.72830 |
56.089 |
0.75100 |
0.83320 |
58.115 |
0.87290 |
0.90415 |
58.902 |
0.94802 |
0.95571 |
59.128 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Sameshima J.: On the System Acetone-Ethyl Ether.. J.Am.Chem.Soc. 40 (1918) 1482-1503 |
Vapor-Liquid Equilibrium Data Set 632
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
9.279 |
0.00000 |
0.00000 |
15.799 |
0.15600 |
0.44600 |
15.599 |
0.19200 |
0.43600 |
18.972 |
0.36400 |
0.61700 |
19.998 |
0.51000 |
0.67000 |
22.238 |
0.61700 |
0.72800 |
24.158 |
0.83500 |
0.86100 |
24.745 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Cunaeus E.H.J.: Die Bestimmung des Brechungsvermögens als Methode zur Untersuchung der Zusammensetzung koexistierender Dampf- und Flüssigkeitsphasen. Z.Phys.Chem.(Leipzig) 36 (1901) 232-238 |
Vapor-Liquid Equilibrium Data Set 633
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
37.690 |
0.00000 |
0.00000 |
39.650 |
0.02010 |
0.06980 |
43.463 |
0.04720 |
0.16960 |
45.036 |
0.06630 |
0.21010 |
54.609 |
0.16190 |
0.40660 |
63.955 |
0.29530 |
0.55450 |
67.021 |
0.34930 |
0.59970 |
74.367 |
0.50420 |
0.69960 |
79.593 |
0.65460 |
0.77820 |
82.247 |
0.74910 |
0.82700 |
84.926 |
0.86730 |
0.89600 |
86.033 |
0.96133 |
0.96625 |
86.126 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Sameshima J.: On the System Acetone-Ethyl Ether.. J.Am.Chem.Soc. 40 (1918) 1482-1503 |
Diagrams
List of All References
Source |
Cunaeus E.H.J.: Die Bestimmung des Brechungsvermögens als Methode zur Untersuchung der Zusammensetzung koexistierender Dampf- und Flüssigkeitsphasen. Z.Phys.Chem.(Leipzig) 36 (1901) 232-238 |
Sameshima J.: On the System Acetone-Ethyl Ether.. J.Am.Chem.Soc. 40 (1918) 1482-1503 |
Vapor-Liquid Equilibrium Data Overview
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