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 1332
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
19.065 |
0.00000 |
0.00000 |
19.065 |
0.10000 |
0.09800 |
19.065 |
0.20000 |
0.22400 |
20.132 |
0.30000 |
0.39700 |
22.132 |
0.40000 |
0.57200 |
25.731 |
0.50000 |
0.74100 |
30.664 |
0.60000 |
0.85200 |
36.397 |
0.70000 |
0.91900 |
42.263 |
0.80000 |
0.95900 |
47.996 |
0.90000 |
0.98300 |
50.529 |
0.95000 |
0.99240 |
52.982 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Guglielmo G.: Sulle Tensioni Parziali e le Pressioni Osmotiche delle Miscele di Liquidi Volatili. Rendiconti/Acad.Naz.Lincei Cl.Sci.Fis.Mat.Natur. 1 (1892) 294-298 |
Vapor-Liquid Equilibrium Data Set 2727
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
26.398 |
0.00000 |
0.00000 |
26.331 |
0.01630 |
0.01534 |
26.305 |
0.03269 |
0.03172 |
26.278 |
0.04339 |
0.04241 |
26.265 |
0.05221 |
0.05123 |
26.238 |
0.07199 |
0.07100 |
26.211 |
0.09102 |
0.09203 |
26.198 |
0.10214 |
0.10621 |
26.211 |
0.11232 |
0.11743 |
26.265 |
0.13078 |
0.14216 |
26.265 |
0.13181 |
0.14216 |
26.318 |
0.15255 |
0.16931 |
26.371 |
0.16301 |
0.18619 |
26.438 |
0.17984 |
0.20854 |
26.491 |
0.18301 |
0.21068 |
26.504 |
0.18407 |
0.21389 |
26.944 |
0.23648 |
0.29312 |
27.131 |
0.25163 |
0.31732 |
27.704 |
0.28763 |
0.37825 |
28.438 |
0.31953 |
0.43614 |
28.731 |
0.33168 |
0.45952 |
30.011 |
0.37492 |
0.53610 |
30.677 |
0.39160 |
0.56148 |
32.024 |
0.42946 |
0.62724 |
32.611 |
0.44171 |
0.64465 |
39.130 |
0.55708 |
0.78732 |
39.237 |
0.55928 |
0.79262 |
41.410 |
0.58348 |
0.82647 |
43.503 |
0.61961 |
0.85179 |
43.543 |
0.61961 |
0.85179 |
43.623 |
0.62397 |
0.85495 |
44.663 |
0.63269 |
0.86654 |
50.436 |
0.71052 |
0.91709 |
50.556 |
0.71589 |
0.91920 |
54.502 |
0.75117 |
0.93924 |
54.529 |
0.75437 |
0.94135 |
54.929 |
0.76502 |
0.94241 |
56.182 |
0.78202 |
0.94874 |
56.209 |
0.78202 |
0.95191 |
57.489 |
0.80216 |
0.95826 |
57.502 |
0.80269 |
0.95932 |
59.422 |
0.82542 |
0.96461 |
62.208 |
0.86022 |
0.97522 |
63.888 |
0.88760 |
0.98053 |
71.594 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Becker F.; Kiefer M.; Rhensius P.; Schaefer H.D.: Interpretation von Dampfdruckdiagrammen binärer flüssiger Mischungen mit Hilfe von Gleichgewichtsmodellen. Z.Phys.Chem.(München) 92 (1974) 169-192 |
Vapor-Liquid Equilibrium Data Set 3493
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
8.133 |
0.00000 |
9.333 |
0.10000 |
10.532 |
0.20000 |
11.866 |
0.30000 |
13.332 |
0.40000 |
14.532 |
0.50000 |
16.265 |
0.60000 |
18.265 |
0.70000 |
20.132 |
0.80000 |
22.398 |
0.90000 |
24.971 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Schmidt G.C.: Binäre Gemische. Z.Phys.Chem.(Leipzig) 121 (1926) 221-253 |
Diagrams
List of All References
Source |
Becker F.; Kiefer M.; Rhensius P.; Schaefer H.D.: Interpretation von Dampfdruckdiagrammen binärer flüssiger Mischungen mit Hilfe von Gleichgewichtsmodellen. Z.Phys.Chem.(München) 92 (1974) 169-192 |
Guglielmo G.: Sulle Tensioni Parziali e le Pressioni Osmotiche delle Miscele di Liquidi Volatili. Rendiconti/Acad.Naz.Lincei Cl.Sci.Fis.Mat.Natur. 1 (1892) 294-298 |
Schmidt G.C.: Binäre Gemische. Z.Phys.Chem.(Leipzig) 121 (1926) 221-253 |
Vapor-Liquid Equilibrium Data Overview
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