In order to recover potassium from sea water and brine, a study was made on the mechanism of selective adsorption of potassium by using irorganic ion exchangers. In this study were examined the effects on the selective adsorption of pH, temperature, composition and concentration of the raw solution, and also the effect of the molar ratio of phosphate to zirconium (P/Zr) in the preparation of these exchangers. The Kinds of exchangers prepared were as follows:
Zirconium phosphate:
Amorphous (ZP)
Crystalline (CZP)
Zirconium Polyphosphate:(ZPP)
Zirconium tripolyphosphate
Zirconium pyrophosphate
Zirconium trimetaphosphate
Zirconium hexametaphosphate
Zirconium silicate phosphate:(ZSP)
Zirconium tangstate phosphate:(ZWP)
Zirconium molybdate phosphate:(ZMP)
Phospho antimonic acid:(SbP)
(1) All the inorganic ion exchangers test showed selective adsorption properties for potassium dissolved in sea water and brine.
(2) Incase 1g of exchanger was used for 950m
lof brine (16°) produced by ion exchange membrane method, the adsorption capacity of zirconium phosphate for potassium amounted to 25mg K
+/g, and zirconium pyrophosphate proved to be the best capacity among the tested exchangers.
(3) The selective adsorption property for potassium ion increased with a rise in the drying temperature of exchangers. However, the selectivity decreased with a rise in the temperature of cation exchange reaction. In case the variation of the drying or reaction temperature became greater, exchangers of higher degree of crystallinity showed a greater variation in the adsorption capacity and selectivity. On the other hand, the amorphous exchanger was less influenced by the variation of temperature.
(4) The adsorption rate of potassium ion was found to be the fastest as compared with other cations, and the amount of potassium adsorbed to the saturated capacity for a short time.
(5) The selective adsorption property for potassium, which was evaluated by the selective adsorption coefficient of a cation (i) to potassium ion (α
ik), was classified easily by apparent volume of wett exchanger (ν'). When the value of ν' was less than 1cm
3/g,α
NaK>α
MgK, and when the value was more than 1cm
3/g,α
NaK<α
MgK.
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