EDWARD J . FARKAS University of Waterloo, Waterloo, Ontario and ALEXANDER HIMSLEY Himsley Engineering Limited, Toronto, Ontario on exchange in fixed beds i s a well-established technology. A t t h e same time there is increasing interest in carrying out ion exchange processes i n agitated vessels. The advantages have been discussed frequently"-". Furthermore, a series of agitated vessels of proper design would o f f e r the possibility of continuous operation"), as against t h e cyclic operation necessary with fixed beds. I n an agitated vessel, t h e beads of ion exchange resin a r e suspended in the liquid and can move about freely. However in many respects the process which is occurring in an agitated o r well-mixed bed a n d in a fixed bed is the same. The feed i s a solution containing concentration C, of the ion to be transferred. Consider t h a t a t time t = 0 we begin t o feed this solution to a mass of resin which is initially free of the ion of interest. It will then be found that the concentration of this ion in the effluent f
The Canadian Journal of Chemical Engineering – Wiley
Published: Jan 1, 1975
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