Hypochlorite leaching of two types of chlorine-alkali sludges was stud
ied. Experiments were carried out to determine the relevant variables
affecting mercury extraction. Ninety seven percent of mercury extracti
on was achieved with experimental conditions of 150 g l-1 NaCl, 35-deg
rees-C temperature, 0.26% (w/w) active chlorine, a solid/liquid ratio
(w/w) of 0.30 and a stirring speed of 1050 rpm. The effects of reactor
geometry, type of agitator and consumption of acid and chlorine durin
g leaching were analysed. A relationship was established between the m
ercury in the leaching solution and in the solid under equilibrium con
ditions.