In Japan, common table salt has been manufactured by evaporating concentrated seawater (i. e., nic brine), produced by electrodialysis using ion-exchange membranes, since 1972. The present dy was conducted to obtain fundamental data on the treatment of ionic brine and its bittern salt factories.
The compositions of ionic brine produced at various Japanese salt factories and laboratories re examined and their properties clarified.
Solubility equilibria for a quinary system of Na
+, K
+, Mg
2+, Ca
2||Cl
--H
2O and the surrounding stems were determined by the isothermal method at 0.25, and 100°C. On the basis of the exrimental results and published data, various phase diagrams for quaternary and quinary systems re drawn.
To estimate liquid composition, at NaCl saturation, for the quinary system of Na
+, K
+, Mg
2+, Ca
2+Cl
--H
2O, generalized equations were derived and verified by experiment. A new metho s developed to provide visual representation of the three-dimensional field of NaCl crystallization, rmally shown using tetrahedral coordinates for the quinary system, by simple triangular coordites. The validity of this method was confirmed experimentally.
Graphical calculations for the isothermal evaporation of ionic brine at 25°C were made. Values changes in the liquid phase components and types of crystals deposited were found to be fficiently reliable by comparison with experimental data.
A method of graphical calculation was devised for the treatment of ionic brine in salt factories, th respect to salt deposition by the evaporation of ionic brine and cooling the hot mother liquor d other procedures. The application of this method to the salt manufacturing process is disssed.
It was concluded that the above results provide an adequate basis for establishing optimum erating conditions for salt production from brine obtained by the ion-exchange membrane method.
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