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 4005
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
3 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
Search the DDB for all data of this mixture
Data Table
T [K] |
xL1 [mol/mol] |
xL2 [mol/mol] |
300.65 |
0.87554 |
0.09061 |
312.65 |
0.85673 |
0.08866 |
320.95 |
0.83348 |
0.08624 |
323.95 |
0.82074 |
0.08491 |
329.05 |
0.78726 |
0.08145 |
333.35 |
0.74316 |
0.07689 |
337.95 |
0.66787 |
0.06912 |
342.55 |
0.41540 |
0.04298 |
305.65 |
0.77511 |
0.19575 |
318.35 |
0.75789 |
0.19139 |
330.05 |
0.72008 |
0.18185 |
332.15 |
0.70732 |
0.17863 |
335.75 |
0.67205 |
0.16971 |
342.25 |
0.47771 |
0.12063 |
344.25 |
0.34424 |
0.08692 |
316.15 |
0.71470 |
0.24729 |
333.04 |
0.66980 |
0.23176 |
337.38 |
0.63419 |
0.21941 |
341.22 |
0.55445 |
0.19183 |
342.39 |
0.49693 |
0.17192 |
343.02 |
0.46129 |
0.15960 |
344.18 |
0.38004 |
0.13151 |
344.25 |
0.37801 |
0.13080 |
345.49 |
0.27048 |
0.09358 |
343.95 |
0.44008 |
0.20292 |
344.93 |
0.36750 |
0.16945 |
349.95 |
0.05595 |
0.025795 |
344.79 |
0.40544 |
0.22278 |
317.49 |
0.61234 |
0.36174 |
324.26 |
0.60617 |
0.35811 |
342.56 |
0.52402 |
0.30957 |
344.22 |
0.45857 |
0.27091 |
344.63 |
0.42446 |
0.25074 |
344.65 |
0.41929 |
0.24770 |
350.95 |
0.03326 |
0.019634 |
352.42 |
0.012693 |
0.00750 |
333.19 |
0.55740 |
0.39332 |
342.17 |
0.51933 |
0.36646 |
344.75 |
0.47109 |
0.39592 |
343.15 |
0.48991 |
0.41638 |
343.49 |
0.48868 |
0.41535 |
344.46 |
0.47602 |
0.40459 |
344.79 |
0.46892 |
0.39855 |
322.35 |
0.49038 |
0.49216 |
336.45 |
0.48146 |
0.48320 |
339.95 |
0.47467 |
0.47639 |
343.95 |
0.46139 |
0.46306 |
344.55 |
0.45839 |
0.46007 |
344.95 |
0.45507 |
0.45671 |
352.75 |
0.00770 |
0.007733 |
344.94 |
0.45585 |
0.45797 |
345.08 |
0.45402 |
0.45612 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
Source |
Mannhardt O.W.; de Right R.E.; Martin W.H.; Burmaster C.F.; Wadt W.F.: The Solubility of Naphthalene in Aqueous Solutions of Methanol, Ethanol, 1-Propanol, and 1-Butanol at Several Temperatures. J.Phys.Chem. 47 (1943) 685-701 |
Solid-Liquid Equilibrium Data Set 5543
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
3 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
Search the DDB for all data of this mixture
Data Table
T [K] |
xL1 [mol/mol] |
xL2 [mol/mol] |
275.25 |
0.01590 |
0.98410 |
283.85 |
0.01590 |
0.98410 |
289.25 |
0.01590 |
0.98410 |
294.85 |
0.01590 |
0.98409 |
298.25 |
0.01590 |
0.98409 |
303.75 |
0.01590 |
0.98409 |
308.15 |
0.01590 |
0.98409 |
312.95 |
0.01590 |
0.98409 |
318.05 |
0.01590 |
0.98409 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
Source |
Bennett D.; Canady W.J.: Thermodynamics of Solution of Naphthalene in Various Water-Ethanol Mixtures. J.Am.Chem.Soc. 106 (1984) 910-915 |
Solid-Liquid Equilibrium Data Set 5544
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
3 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
Search the DDB for all data of this mixture
Data Table
T [K] |
xL1 [mol/mol] |
xL2 [mol/mol] |
275.00 |
0.03290 |
0.96710 |
283.85 |
0.03290 |
0.96710 |
288.74 |
0.03290 |
0.96710 |
294.85 |
0.03290 |
0.96709 |
298.55 |
0.03290 |
0.96709 |
303.65 |
0.03290 |
0.96709 |
313.15 |
0.03290 |
0.96709 |
317.55 |
0.03290 |
0.96708 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
Source |
Bennett D.; Canady W.J.: Thermodynamics of Solution of Naphthalene in Various Water-Ethanol Mixtures. J.Am.Chem.Soc. 106 (1984) 910-915 |
Solid-Liquid Equilibrium Data Overview
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