The stoichiometry and kinetics of Co2+ reduction with NaBH4 in aqueous
solution have been studied. A substantial excess of borohydride is ne
eded to achieve complete Co2+ removal from water, mainly due to borohy
dride consumption in the BH4-/H2O reaction unless the pH is sufficient
ly alkaline. In this case, cobalt precipitation occurs mainly as Co(OH
)2. Absence of dissolved oxygen in the reactor is required to avoid ra
pid reoxidation.of reduced cobalt. The elemental analysis of the reduc
ed species is consistent with Co2B. The ease of sludge reoxidation and
the final boron concentration in the effluent resulting from the need
ed excess of borohydride are serious disadvantages of this technique f
or Co2+ removal. A kinetic model has been proposed to describe the beh
aviour of the system. The model reproduces reasonably well the experim
ental results, although some discrepancies were observed in the early
stages of the process. These can be mainly attributed to mass-transfer
limitations.