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 408
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
353.15 |
0.05000 |
0.06000 |
352.95 |
0.08000 |
0.10000 |
352.35 |
0.12000 |
0.15000 |
351.65 |
0.20000 |
0.27000 |
350.15 |
0.32000 |
0.44500 |
349.45 |
0.38000 |
0.52000 |
348.45 |
0.45000 |
0.61000 |
346.65 |
0.56000 |
0.71000 |
345.45 |
0.64000 |
0.78000 |
342.15 |
0.78000 |
0.89000 |
341.15 |
0.82000 |
0.91000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Bukala M.; Majewski J.: Dwupolkowy aparat do oznaczania stanu rownowagi ciecz-para pod cisnieniem normalnym i zmniejszonym. Przem.Chem. 8 (1952) 551-554 |
Vapor-Liquid Equilibrium Data Set 409
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
14.119 |
0.13400 |
0.21800 |
15.732 |
0.28400 |
0.42400 |
16.732 |
0.36000 |
0.53000 |
20.718 |
0.62800 |
0.80400 |
22.665 |
0.74000 |
0.88600 |
24.785 |
0.86600 |
0.95000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Kireev V.A.; Sitnikov I.P.: Benzol - Chloroform - Mischungen. Zh.Obshch.Khim. 16 (1946) 979-982 |
Vapor-Liquid Equilibrium Data Set 410
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
352.35 |
0.06000 |
0.08900 |
352.15 |
0.06800 |
0.10000 |
351.55 |
0.11600 |
0.16700 |
351.05 |
0.13300 |
0.19000 |
350.05 |
0.19300 |
0.27000 |
349.35 |
0.22900 |
0.31600 |
348.85 |
0.26600 |
0.36100 |
347.85 |
0.31800 |
0.42900 |
347.55 |
0.33300 |
0.44300 |
346.45 |
0.38800 |
0.50800 |
345.35 |
0.44300 |
0.57000 |
344.75 |
0.46700 |
0.60100 |
343.95 |
0.51700 |
0.65200 |
342.85 |
0.57000 |
0.70200 |
341.45 |
0.63700 |
0.76200 |
340.15 |
0.70000 |
0.81400 |
338.55 |
0.78300 |
0.87500 |
337.25 |
0.85300 |
0.92200 |
335.75 |
0.93400 |
0.96800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Nagata I.: Vapor-Liquid Equilibrium at Atmospheric Pressure for the Ternary System Methyl Acetate-Chloroform-Benzene. J.Chem.Eng.Data 7 (1962) 360-366 |
Diagrams
List of All References
Source |
Bukala M.; Majewski J.: Dwupolkowy aparat do oznaczania stanu rownowagi ciecz-para pod cisnieniem normalnym i zmniejszonym. Przem.Chem. 8 (1952) 551-554 |
Kireev V.A.; Sitnikov I.P.: Benzol - Chloroform - Mischungen. Zh.Obshch.Khim. 16 (1946) 979-982 |
Nagata I.: Vapor-Liquid Equilibrium at Atmospheric Pressure for the Ternary System Methyl Acetate-Chloroform-Benzene. J.Chem.Eng.Data 7 (1962) 360-366 |
Vapor-Liquid Equilibrium Data Overview
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