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Additional info for Inorganic Syntheses, Vol. 30: Nonmolecular Solids
In analyzing schemes for separation processes the separation of component mixtures or the purification of components with sorbability extremes (lowestor highest) from multicomponent systems willbe considered. When separating multicomponent mixtures the problem of providing flow circulation is solved in the same way as in separating twocomponent mixtures. 11. SEPARATIONPROCESSES WITH FLOW REVERSAL A general scheme for the countercurrention-exchange separation process with flow reversal is analogous to the schemes for such two-phase separation processes as rectification, ,chemical exchange, etc.
Purification from Impurities Sorbed More Strongly than the Substance to Be Purified The product BX, with decreased content of impurities, is obtained in column I. Carried out in columnI1 is the combined processof separation and recovery of the AX and BX mixture fromthe ion exchangerand resin regeneration. The process scheme is shownin Fig. 3. For complete displacement of the ions separated by the auxiliary C ions in columnI1 it is necessary  that the ratio of solution and ion exchanger flow inputs should satisfy the condition where = y(1- x)/(l - y)x, and y and xare equivalent fractionsof A in the ion exchanger and solution, respectively,at equilibrium.
3171, or for the puritication of nickel from calciumon cation exchanger [M]. Similarly the process may also be performed when the purpose is to obtain A as AX. The recovery of Rb+ from its mixture withK+, using NH: as an auxiliary ion, canbe used as an example [l91 of this. In the scheme in question the processes of recovery of a given component from ion exchanger and resin regeneration are combined. However, some difficulties may arise when removing CX from the solution leaving column11. With ion exchangerhaving a high affinityfor the ions GORSHKOV L A scheme for purification of product more strongly sorbed im- purities.