The demand for the new development of specific separation techniques for th
e treatment of drinking water leads to re-examining the use of cyclic opera
tions in ion exchange processes. Establishing stable limit fronts inside th
e column is the required condition to allow the use of two-way chromatograp
hy methods and insure the process efficiency. This paper presents numerical
simulations and experimental validation at a laboratory pilot scale showin
g the development of a set of stationary composition profiles during a cycl
ic operation of a chromatographic ion-exchange cyclic process. It has been
shown numerically that stable cycles are obtained in the case where the cut
points are chosen following a criterion based on the breakthrough volumes.
The properties displayed by means of numerical simulations were experiment
ally validated. Reconstituted waters were treated by the cyclic process in
order to selectively eliminate fluoride ion. The process uses two anion-exc
hange columns pre-equilibrated with the hydrogen carbonate anion in excess
in the feed solution. After some cycles, steady concentrations of the major
species (chloride and sulphate ions) are measured: a stable limit cycle is
reached and the condition to (i) eliminate fluoride anion, (ii) restore th
e matrix of the other anions is fulfilled. (C) 2000 Published by Elsevier S
cience Ltd. All rights reserved.