Pk. Sinha et al., APPLICATION OF COMMERCIAL ZEOLITE-13X IN THE TREATMENT OF SIMULATED AND ACTUAL RADIOACTIVE EFFLUENT CONTAINING CESIUM, Indian journal of chemistry. Sect. A: Inorganic, physical, theoretical & analytical, 33(10), 1994, pp. 924-928
The removal of Cs+ ions from aqueous solution and radioactive effluent
, by ion-exchange with Na ions of indigenously available synthetic zeo
lite-13X, has been studied. The zeolite has been characterized with re
spect to chemical composition, stability to acid, XRD and IR spectral
patterns. Batch studies on the kinetics of the Cs-Na exchange process
indicate that at higher Cs concentrations in solution, such as 50 mM a
nd 100 mM Cs, 'particle diffusion' is the controlling factor, as infer
red from the observed linearity in the Bt-t plots. The linearity is ab
sent in case of lower concentrations where the process may be controll
ed by 'film diffusion'. The K-d value are of the order of a few thousa
nds to a few tens of ml/g, depending on the initial concentration of t
he Cs ions. Agitation affected the kinetics in such a way that the tim
e required for attainment of equilibrium is reduced from about 48 h in
an unstirred solution to 2 h in a thoroughly stirred solution. Equili
brium studies, carried out under isonormal solution conditions at two
different total (Cs + Na) ionic concentrations, 0.025 N and 0.1 N, res
ulted into 'adsorption isotherms' showing replacement of 35% and 50% o
f the exchangeable Na+ ions for the two cases, respectively. The colum
n studies, conducted with a pure solution of Cs-137 in ordinary water
and a 2g ( = 3 ml) column of the zeolite,]ed to a removal of as high a
s 99.9% Cs-137. When an actual radioactive waste solution, received fr
om the Madras Atomic Power Station, Kalpakkam, and containing predomin
antly Cs-137, is passed through a 1g( = 1.5 ml) bed of zeolite-13X, th
e per cent breakthrough is found to be less than 4% (96% removal) till
the passage of 1000 bed volumes.