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 590

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H6O 46.069 64-17-5 Ethanol
2 C6H6 78.114 71-43-2 Benzene
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Data Table

T [K] xL1 [mol/mol]
278.65 0.00000
275.65 0.15987
274.25 0.29876
272.75 0.42087
270.55 0.53093
267.05 0.62997
262.05 0.71864
252.15 0.79856
233.65 0.87137
207.15 0.93870
159.15 1.00000

(P - pressure, T - temperature, xl - liquid mole fraction)

Reference

Source
Tarasenkov D.: Gefriertemperatur der Mischungen von Benzol mit Toluol, Alkohol und Benzin. Zh.Prikl.Khim. 3 (1930) 153-155

Solid-Liquid Equilibrium Data Set 1372

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H6O 46.069 64-17-5 Ethanol
2 C6H6 78.114 71-43-2 Benzene
Search the DDB for all data of this mixture

Data Table

T [K] xL1 [mol/mol]
278.65 0.00000
276.45 0.09520
275.45 0.15490
275.15 0.19330
274.65 0.26080
274.15 0.29780
273.90 0.33210
272.90 0.39940
271.95 0.45720
270.85 0.51960
269.55 0.57190
267.75 0.62250
265.50 0.66570
259.45 0.75000
248.95 0.82420
245.65 0.84110
242.15 0.85640
233.15 0.88880
223.15 0.91890
209.85 0.94730
178.15 0.97330
160.35 0.98730
159.25 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 2422

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H6O 46.069 64-17-5 Ethanol
2 C6H6 78.114 71-43-2 Benzene
Search the DDB for all data of this mixture

Data Table

T [K] xL1 [mol/mol]
277.11 0.04057
276.37 0.08184
275.84 0.12208
275.44 0.15885
274.83 0.21844
274.81 0.21844
274.24 0.27414
273.83 0.31907
273.39 0.35227
273.02 0.38832
272.48 0.42185
272.01 0.45395
271.50 0.48298
271.37 0.48975
270.98 0.50687
270.26 0.53241
270.07 0.54107
269.51 0.56233
268.72 0.58276
267.62 0.61347
266.74 0.63123
265.57 0.65749
264.17 0.67957
262.70 0.70221
261.46 0.71985
260.92 0.72102
259.48 0.74274
257.25 0.76044
255.31 0.78180
252.18 0.79779
247.99 0.82220
243.79 0.83711
243.94 0.83711
239.14 0.85806
236.14 0.87180
231.84 0.88313
230.39 0.89601
225.64 0.90601
223.89 0.91422
218.89 0.92089
215.99 0.93080
213.64 0.93853
207.29 0.94617
202.14 0.95393

(P - pressure, T - temperature, xl - liquid mole fraction)

Reference

Source
Pickering S.U.: A Study of the Properties of some Strong Solutions. J.Chem.Soc.London 63 (1893) 998-1027

Diagrams

Solid-Liquid Equilibrium of Ethanol+Benzene
See larger image

Solid-Liquid Equilibrium Data Overview


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