The biosorption of Cu, Cd, and Zn from multicomponent mixtures was studied
in equilibrium systems and in a flow-through column packed with potassium-s
aturated Sargassum algal biosorbent. Pretreatment of the biomass with calci
um-, sodium-, magnesium-, and potassium-hydroxides was examined. KOH washin
g resulted in a stable biosorbent with an improved affinity for Zinc. Two-m
etal sorption resulted in Zn breaking through the column faster than Cd due
to its low affinity. The sharp favorable Zn breakthrough curve can be expl
ained by its affinity toward the biomass which is higher than that of K. An
overshoot of the Zn exit concentration was observed and explained by the i
on exchange between Cd and Zn, whereby the higher-affinity Cd from the solu
tion displaces Zn already bound to the biosorbent. The same effect was obse
rved for Zn, and to a lesser extent Cd, in three-metal sorption (Zn, Cd, Cu
). The Cd exit concentration also exceeded its feed level as Cu displaced i
t on the binding sites of the biomass in the bed. The time interval between
Zn and Cd breakthroughs was much shorter than that between the breakthroug
h points of Cd and Cu. This is because the relative affinities of Zn and Cd
, determined from batch equilibrium experiments, are much closer to each ot
her (Zn/K = 1.96 and Cd/K = 3.71) than to Cu (Cu/K = 16.51). The applicatio
n of experimental IMPACT computer software examined was only partially succ
essful in exactly simulating the biosorption column performance.