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 1960
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
3 |
H2O |
18.015 |
7732-18-5 |
Water |
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Data Table
T [K] |
xL1 [mol/mol] |
xL2 [mol/mol] |
278.15 |
2.439999889E-6 |
0.00000 |
278.15 |
3.01E-6 |
0.023215 |
278.15 |
3.520000064E-6 |
0.04337 |
278.15 |
4.129999979E-6 |
0.06437 |
278.15 |
5.23000017E-6 |
0.08237 |
278.15 |
6.57999999E-6 |
0.10068 |
283.15 |
2.849999873E-6 |
0.00000 |
283.15 |
3.579999884E-6 |
0.023215 |
283.15 |
4.179999905E-6 |
0.04337 |
283.15 |
5.219999821E-6 |
0.06437 |
283.15 |
6.429999758E-6 |
0.08237 |
283.15 |
8.469999557E-6 |
0.10068 |
288.15 |
3.429999879E-6 |
0.00000 |
288.15 |
4.380000064E-6 |
0.023215 |
288.15 |
5.360000159E-6 |
0.04337 |
288.15 |
6.390000181E-6 |
0.06437 |
288.15 |
8.469999557E-6 |
0.08237 |
288.15 |
1.108000015E-5 |
0.10068 |
293.15 |
4.040000022E-6 |
0.00000 |
293.15 |
5.500000043E-6 |
0.023215 |
293.15 |
6.390000181E-6 |
0.04337 |
293.15 |
7.640000149E-6 |
0.06437 |
293.15 |
1.043999964E-5 |
0.08237 |
293.15 |
1.35600003E-5 |
0.10068 |
298.15 |
4.749999789E-6 |
0.00000 |
298.15 |
6.390000181E-6 |
0.023215 |
298.15 |
7.56999998E-6 |
0.04337 |
298.15 |
9.649999811E-6 |
0.06437 |
298.15 |
1.255000006E-5 |
0.08237 |
298.15 |
1.707000047E-5 |
0.10068 |
303.15 |
5.84999998E-6 |
0.00000 |
303.15 |
7.560000086E-6 |
0.023215 |
303.15 |
9.360000149E-6 |
0.04337 |
303.15 |
1.145999977E-5 |
0.06437 |
303.15 |
1.560999954E-5 |
0.08237 |
303.15 |
2.203000076E-5 |
0.10068 |
308.15 |
6.700000085E-6 |
0.00000 |
308.15 |
8.580000213E-6 |
0.023215 |
308.15 |
1.040000006E-5 |
0.04337 |
308.15 |
1.358000009E-5 |
0.06437 |
308.15 |
1.732999954E-5 |
0.08237 |
308.15 |
2.651000068E-5 |
0.10068 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
Source |
Perez-Tejeda P.; Yanes C.; Maestre A.: Solubility of Naphthalene in Water + Alcohol Solutions at Various Temperatures. J.Chem.Eng.Data 35 (1990) 244-246 |
Solid-Liquid Equilibrium Data Set 4004
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
3 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
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Data Table
T [K] |
xL1 [mol/mol] |
xL2 [mol/mol] |
308.82 |
0.89969 |
0.07626 |
323.75 |
0.87933 |
0.07454 |
336.98 |
0.81651 |
0.06920 |
339.91 |
0.76842 |
0.06512 |
343.31 |
0.54835 |
0.04649 |
343.60 |
0.51882 |
0.04398 |
346.83 |
0.20532 |
0.01738 |
341.90 |
0.70890 |
0.09138 |
343.25 |
0.61280 |
0.07898 |
343.53 |
0.57948 |
0.07472 |
343.61 |
0.57344 |
0.07391 |
343.57 |
0.52843 |
0.06812 |
344.20 |
0.49298 |
0.06354 |
344.15 |
0.49123 |
0.06334 |
344.46 |
0.45093 |
0.05814 |
344.55 |
0.43070 |
0.05550 |
344.65 |
0.42430 |
0.05468 |
345.25 |
0.37164 |
0.04789 |
345.53 |
0.32135 |
0.04142 |
346.65 |
0.21193 |
0.02733 |
346.90 |
0.21321 |
0.040275 |
347.09 |
0.20636 |
0.03897 |
339.30 |
0.76504 |
0.15755 |
343.75 |
0.69314 |
0.14276 |
(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 15263
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Data Table
T [K] |
xL1 [mol/mol] |
xL2 [mol/mol] |
298.15 |
3.630090077E-6 |
0.00000 |
298.15 |
3.727370085E-6 |
0.00000 |
298.15 |
6.15036015E-6 |
0.04697 |
298.15 |
7.19530999E-6 |
0.04697 |
298.15 |
1.062790034E-5 |
0.09982 |
298.15 |
1.443490055E-5 |
0.09982 |
298.15 |
2.149079955E-5 |
0.15974 |
298.15 |
2.385980042E-5 |
0.15973 |
298.15 |
5.503190187E-5 |
0.22822 |
298.15 |
6.273770123E-5 |
0.22821 |
298.15 |
0.0001626689918 |
0.30723 |
298.15 |
0.0001447059913 |
0.30723 |
298.15 |
0.0004283609742 |
0.39936 |
298.15 |
0.0004854479921 |
0.39934 |
298.15 |
0.001160150045 |
0.50801 |
298.15 |
0.001270720037 |
0.50796 |
298.15 |
0.003095 |
0.63757 |
298.15 |
0.003479 |
0.63733 |
298.15 |
0.007197 |
0.79393 |
298.15 |
0.008992 |
0.79250 |
298.15 |
0.02060 |
0.97940 |
298.15 |
0.019024 |
0.98098 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
Source |
Morris K.R.: Solubility of Aromatic Compounds in Mixed Solvents. Thesis (1988) |
Solid-Liquid Equilibrium Data Overview
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