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 692
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 |
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Data Table
| T [K] |
xL1 [mol/mol] |
| 268.65 |
0.04164 |
| 262.65 |
0.08906 |
| 253.15 |
0.14354 |
| 243.75 |
0.20679 |
| 236.15 |
0.28112 |
| 229.35 |
0.36971 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Clendenning K.A.: XI. Evaluation of Levo-2,3-Butanediol as a Non-Volatile Antifreeze Compound. Can.J.Res.Sect.F 24 (1946) 249-271 |
Solid-Liquid Equilibrium Data Set 1489
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 |
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Data Table
| T [K] |
xL1 [mol/mol] |
xS1 [mol/mol] |
| 200.60 |
0.64600 |
0.64600 |
| 151.20 |
0.84000 |
0.84000 |
(P - pressure, T - temperature, xl - liquid mole fraction, xs - solid mole fraction)
Reference
| Source |
| Ott J.B.; Goates J.R.; Waite B.A.: (Solid + Liquid) Phase Equilibria and Solid-Hydrate Formation in Water + Methyl, + Ethyl, + Isopropyl, and + Tertiary Butyl Alcohols. J.Chem.Thermodyn. 11 (1979) 739-746 |
Solid-Liquid Equilibrium Data Set 2415
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 |
Search the DDB for all data of this mixture
Data Table
| T [K] |
xL1 [mol/mol] |
| 272.94 |
0.001914500026 |
| 272.71 |
0.003919600043 |
| 272.52 |
0.00577 |
| 272.30 |
0.007763 |
| 271.90 |
0.01171 |
| 271.49 |
0.015712 |
| 271.07 |
0.019868 |
| 270.63 |
0.023925 |
| 270.12 |
0.028075 |
| 269.70 |
0.032285 |
| 269.15 |
0.03654 |
| 268.64 |
0.04086 |
| 268.28 |
0.04457 |
| 267.84 |
0.04807 |
| 267.66 |
0.04943 |
| 267.04 |
0.05445 |
| 266.54 |
0.05810 |
| 266.21 |
0.06082 |
| 265.39 |
0.06610 |
| 264.71 |
0.07081 |
| 264.78 |
0.07100 |
| 264.23 |
0.07455 |
| 263.48 |
0.07901 |
| 262.91 |
0.08375 |
| 262.16 |
0.08875 |
| 260.82 |
0.09685 |
| 259.54 |
0.10424 |
| 257.93 |
0.11363 |
| 256.73 |
0.11981 |
| 254.93 |
0.12951 |
| 252.66 |
0.14423 |
| 250.81 |
0.15537 |
| 248.15 |
0.17304 |
| 246.12 |
0.18979 |
| 243.55 |
0.20598 |
| 241.75 |
0.22339 |
| 240.65 |
0.24047 |
| 238.35 |
0.25837 |
| 235.55 |
0.28837 |
| 233.15 |
0.32063 |
| 231.65 |
0.34690 |
| 230.20 |
0.36938 |
| 228.75 |
0.38821 |
| 228.35 |
0.39929 |
| 227.35 |
0.40847 |
| 226.65 |
0.41626 |
| 226.35 |
0.41754 |
| 225.25 |
0.43027 |
| 225.15 |
0.43324 |
| 223.80 |
0.44921 |
| 221.90 |
0.46635 |
| 221.85 |
0.46953 |
| 220.15 |
0.48496 |
| 219.65 |
0.48863 |
| 217.40 |
0.50167 |
| 217.65 |
0.50477 |
| 216.65 |
0.51962 |
| 214.95 |
0.53177 |
| 213.65 |
0.53996 |
| 213.15 |
0.54044 |
| 212.15 |
0.55018 |
| 211.15 |
0.56026 |
(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 Data Overview
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