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 922
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
208.637 |
0.97286 |
208.635 |
0.97499 |
208.028 |
0.97714 |
206.224 |
0.97825 |
204.261 |
0.97951 |
201.771 |
0.98113 |
199.272 |
0.98195 |
198.072 |
0.98273 |
195.011 |
0.98380 |
189.339 |
0.98574 |
184.108 |
0.98742 |
179.249 |
0.98900 |
171.781 |
0.99087 |
166.836 |
0.99245 |
157.770 |
0.99520 |
151.566 |
0.99682 |
146.259 |
0.99814 |
141.380 |
0.99925 |
138.033 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Fischer K.: Experimentelle Bestimmung der Siedekurve im System Benzol(1)-Wasser(2) im homogenen Benzol - reichen Bereich bei 90.48 °C mit Hilfe der synthetischen statischen Meßmethode. Unpublished Data (1994) 0 |
Vapor-Liquid Equilibrium Data Set 3804
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
12.899 |
0.99740 |
12.386 |
0.99770 |
11.799 |
0.99810 |
11.639 |
0.99850 |
10.998 |
0.99900 |
10.831 |
0.99910 |
10.602 |
0.99930 |
10.566 |
0.99950 |
10.508 |
0.99960 |
10.212 |
0.99970 |
10.136 |
0.99980 |
10.172 |
0.99990 |
10.106 |
0.99990 |
10.083 |
0.99990 |
9.994 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Niini A.: I. Unpolare Lösungsmittel. Suom.Tied.Toimit.Ser.A Sci.Nat. 55 (1940) 1-52 |
Vapor-Liquid Equilibrium Data Set 15335
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
2 |
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] |
y1 [mol/mol] |
373.01 |
0.00000 |
0.00000 |
365.35 |
0.00040 |
0.23200 |
370.90 |
0.00200 |
0.12120 |
367.65 |
0.00670 |
0.18520 |
351.50 |
0.00690 |
0.48060 |
355.15 |
0.00830 |
0.41340 |
342.43 |
0.00870 |
0.68280 |
362.35 |
0.01070 |
0.26110 |
344.88 |
0.01070 |
0.62210 |
357.10 |
0.01230 |
0.35760 |
348.65 |
0.01230 |
0.49700 |
346.74 |
0.01250 |
0.60980 |
342.42 |
0.01680 |
0.70020 |
342.80 |
0.01990 |
0.68600 |
342.42 |
0.02800 |
0.70380 |
343.45 |
0.78550 |
0.70240 |
345.17 |
0.97030 |
0.76650 |
345.99 |
0.98330 |
0.81730 |
348.99 |
0.98710 |
0.88850 |
347.80 |
0.98750 |
0.85640 |
350.87 |
0.99050 |
0.93100 |
352.98 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Tu M.; Lei G.; Fei D.: Phase Equilibrium for the System of Phosphoric Acid - Water - Benzene. Chengdu-Keji-Daxue-Xuebao 3 (1992) 65-70 |
Diagrams
List of All References
Source |
Niini A.: I. Unpolare Lösungsmittel. Suom.Tied.Toimit.Ser.A Sci.Nat. 55 (1940) 1-52 |
Fischer K.: Experimentelle Bestimmung der Siedekurve im System Benzol(1)-Wasser(2) im homogenen Benzol - reichen Bereich bei 90.48 °C mit Hilfe der synthetischen statischen Meßmethode. Unpublished Data (1994) 0 |
Tu M.; Lei G.; Fei D.: Phase Equilibrium for the System of Phosphoric Acid - Water - Benzene. Chengdu-Keji-Daxue-Xuebao 3 (1992) 65-70 |
Vapor-Liquid Equilibrium Data Overview
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