Dortmund Data Bank
Solid-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.
Solid-Liquid Equilibrium Data Set 1374
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Data Table
| T [K] |
xL1 [mol/mol] |
| 278.55 |
0.00000 |
| 277.25 |
0.03400 |
| 274.90 |
0.15290 |
| 274.15 |
0.18970 |
| 273.70 |
0.25250 |
| 273.05 |
0.31440 |
| 271.90 |
0.38990 |
| 271.15 |
0.42450 |
| 269.35 |
0.50120 |
| 268.40 |
0.54540 |
| 267.05 |
0.58000 |
| 264.25 |
0.62720 |
| 262.15 |
0.66330 |
| 257.85 |
0.71830 |
| 249.95 |
0.79840 |
| 242.15 |
0.84540 |
| 226.15 |
0.91140 |
| 212.15 |
0.96730 |
| 192.15 |
0.98640 |
| 195.15 |
1.00000 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Perrakis N.: Les propriétés physiques des mélanges doubles liquides dans le voisinage de l'état critique de miscibilité. J.Chim.Phys. 22 (1925) 280-310 |
Solid-Liquid Equilibrium Data Set 50563
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Data Table
| T [K] |
xL1 [mol/mol] |
| 277.07 |
0.04040 |
| 277.14 |
0.03759 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Izmailov N.A.; Tsarevskaya M.N.: 4. Physico-Chemical Analisis in Solutions and Calculation of Reaction Yield. Ukr.Khim.Zh.(Russ.Ed.) 26 (1960) 688-696 |
Solid-Liquid Equilibrium Data Set 50988
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Data Table
| T [K] |
xL1 [mol/mol] |
| 278.60 |
0.00078 |
| 278.55 |
0.00156 |
| 278.50 |
0.00234 |
| 278.46 |
0.00311 |
| 278.41 |
0.00389 |
| 278.19 |
0.00775 |
| 277.99 |
0.01158 |
| 277.81 |
0.01538 |
| 277.66 |
0.01915 |
| 277.53 |
0.02290 |
| 277.41 |
0.02661 |
| 277.32 |
0.03030 |
| 277.23 |
0.03396 |
| 277.14 |
0.03759 |
| 277.05 |
0.04119 |
| 276.96 |
0.04477 |
| 276.89 |
0.04832 |
| 276.81 |
0.05184 |
| 276.75 |
0.05534 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Izmailov N.A.; Franke A.K.: III. Interaction of carbonic acids with butanol. Ukr.Khim.Zh.(Russ.Ed.) 22 (1956) 557-566 |
Diagrams
Solid-Liquid Equilibrium Data Overview
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