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 5667
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H6 |
54.092 |
106-99-0 |
1,3-Butadiene |
2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
16.212 |
0.00000 |
0.00000 |
25.331 |
0.03600 |
0.48000 |
50.663 |
0.12000 |
0.81600 |
101.325 |
0.28000 |
0.92000 |
202.650 |
0.60000 |
0.98000 |
303.975 |
0.92000 |
0.99800 |
333.359 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Rozhnov M.S.: Phasen- und Volumenverhältnisse in Systemen Divinyl-Kohlenwasserstoffe. Khim.Prom. 43 (1967) 288-290 |
Vapor-Liquid Equilibrium Data Set 10955
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H6 |
54.092 |
106-99-0 |
1,3-Butadiene |
2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
72.549 |
0.00000 |
0.00000 |
101.325 |
0.03200 |
0.33600 |
202.650 |
0.15200 |
0.73200 |
303.975 |
0.26400 |
0.86200 |
405.300 |
0.38000 |
0.91600 |
506.625 |
0.50000 |
0.94800 |
607.950 |
0.61600 |
0.96800 |
709.275 |
0.72800 |
0.98200 |
810.600 |
0.84400 |
0.99400 |
911.925 |
0.96000 |
0.99800 |
949.415 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Rozhnov M.S.: Phasen- und Volumenverhältnisse in Systemen Divinyl-Kohlenwasserstoffe. Khim.Prom. 43 (1967) 288-290 |
Vapor-Liquid Equilibrium Data Set 12916
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H6 |
54.092 |
106-99-0 |
1,3-Butadiene |
2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
225.955 |
0.00000 |
0.00000 |
253.313 |
0.02000 |
0.14800 |
405.300 |
0.10600 |
0.56800 |
607.950 |
0.22400 |
0.75600 |
810.600 |
0.34400 |
0.84000 |
1013.250 |
0.46000 |
0.89600 |
1215.900 |
0.58000 |
0.93600 |
1418.550 |
0.69600 |
0.96200 |
1621.200 |
0.80800 |
0.98000 |
1823.850 |
0.90400 |
0.99200 |
2026.500 |
0.98200 |
0.99800 |
2093.375 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Rozhnov M.S.: Phasen- und Volumenverhältnisse in Systemen Divinyl-Kohlenwasserstoffe. Khim.Prom. 43 (1967) 288-290 |
Diagrams
List of All References
Source |
Rozhnov M.S.: Phasen- und Volumenverhältnisse in Systemen Divinyl-Kohlenwasserstoffe. Khim.Prom. 43 (1967) 288-290 |
Vapor-Liquid Equilibrium Data Overview
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