Abstract
Lead and cadmium removal from aqueous solution by batch ion exchange with a solid NaY zeolite has been studied under competitive and non-competitive conditions. The extent of heavy metal (HM) removal is found to be inlependent of the nature of the anion, and equilibrium exchange isotherms are presented for NaY treatment of lead and cadmium nitrate and chloride solutions at 293 K. An increase in solution phase HM concentration lowers the affinity of the zeolite for the in-going HM ion, but lead was preferred to the indigenous sodium ion over the entire range of initial metal concentration to zeolite weight ratios (0.3–13 × 10−2 mol dm−3 gz−1) that were studied. Lead removal was much greater than that of cadmium under identical experimental conditions and NaY exchange efficiency is shown to increase in the order Ni2+ < Cu2+ < Cd2+ < Pb2+. Exchange selectivity is discussed in terms of metal ion hydration and siting within the zeolite framework. A Pb/Cd/NaY ternary exchange isotherm was constructed from 38 pairs of experimental points, and is treated quantitatively in terms of ternary and pseudo-binary separation factors. Treatment of the lead/cadmium solutions resulted in a greater depletion (by a factor of 2) of the lead component.
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