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 15302

Components

No. Formula Molar Mass CAS Registry Number Name
1 C10H8 128.174 91-20-3 Naphthalene
2 H2O 18.015 7732-18-5 Water
3 C2H3N 41.053 75-05-8 Acetonitrile
4 CH4O 32.042 67-56-1 Methanol
Search the DDB for all data of this mixture

Data Table

T [K] xL1 [mol/mol] xL2 [mol/mol] xL3 [mol/mol]
298.15 3.62365995E-6 1.00000 0.00000
298.15 7.839060345E-6 0.95359 0.00000
298.15 3.47464993E-5 0.90129 0.00000
298.15 0.0001410200057 0.84185 0.00000
298.15 0.0004462109937 0.77367 0.00000
298.15 0.001127 0.69465 0.00000
298.15 0.004037 0.60110 0.00000
298.15 0.008561 0.49036 0.00000
298.15 0.01520 0.35788 0.00000
298.15 0.028366 0.19663 0.00000
298.15 0.05533 0.00000 0.00000
298.15 6.737629974E-6 0.96295 0.037046
298.15 1.719699867E-5 0.91071 0.039416
298.15 0.00018795699 0.85120 0.04210
298.15 0.0002370309958 0.78310 0.04519
298.15 0.001041249954 0.70369 0.04873
298.15 0.002646530047 0.61038 0.05283
298.15 0.006029 0.49916 0.05761
298.15 0.012315 0.36501 0.06319
298.15 0.02469 0.20110 0.06963
298.15 0.04953 0.00000 0.07675
298.15 1.288230033E-5 0.92032 0.07966
298.15 4.159269884E-5 0.86093 0.08517
298.15 0.000173812994 0.79264 0.09148
298.15 0.000747 0.71311 0.09876
298.15 0.001443249988 0.61981 0.10730
298.15 0.004244 0.50785 0.11723
298.15 0.010204 0.37209 0.12883
298.15 0.021013 0.20575 0.14248
298.15 0.05167 0.00000 0.15651
298.15 2.013489939E-5 0.87077 0.12921
298.15 9.449130448E-5 0.80242 0.13892
298.15 0.0004777069844 0.72276 0.15015
298.15 0.001398249995 0.62879 0.16329
298.15 0.003933 0.51605 0.17868
298.15 0.009054 0.37906 0.19687
298.15 0.021417 0.20971 0.21783
298.15 0.04428 0.00000 0.24187
298.15 5.257399971E-5 0.81242 0.18753
298.15 0.0002163089957 0.73267 0.20294
298.15 0.001052 0.63822 0.22098
298.15 0.00325040007 0.52472 0.24224
298.15 0.007853 0.38629 0.26750
298.15 0.019954 0.21423 0.29671
298.15 0.044265 0.00000 0.32988
298.15 0.0001663329895 0.74269 0.25715
298.15 0.0006006949698 0.64800 0.28045
298.15 0.002566 0.53366 0.30796
298.15 0.008368 0.39311 0.34028
298.15 0.017377 0.21919 0.37946
298.15 0.03964 0.00000 0.42403
298.15 0.000519 0.65783 0.34165
298.15 0.001765229972 0.54297 0.37600
298.15 0.005647 0.40149 0.41704
298.15 0.014137 0.22450 0.46640
298.15 0.03967 0.00000 0.52100
298.15 0.001362239942 0.55238 0.44626
298.15 0.004575 0.40950 0.49625
298.15 0.013484 0.22944 0.55610
298.15 0.038845 0.00000 0.62328
298.15 0.003793 0.41770 0.57850
298.15 0.011225 0.23498 0.65088
298.15 0.03186 0.00000 0.73555
298.15 0.00956 0.24062 0.74982
298.15 0.02987 0.00000 0.85059
298.15 0.02449 0.00000 0.97551

(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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