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
Search the DDB for all data of this mixture

Constant Value

Temperature 290.55 K

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
Search the DDB for all data of this mixture

Constant Value

Temperature 298.15 K

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
Search the DDB for all data of this mixture

Constant Value

Temperature 273.15 K

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

Vapor-Liquid Equilibrium of Diethyl ether+Chloroform
See larger image
Vapor-Liquid Equilibrium of Diethyl ether+Chloroform
See larger image

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


© DDBST GmbH