The electrochemical regeneration of chromium containing solution obtained from metal finishing industry
was carried out using different anode materials (lead & platinished titanium) and cathode materials (lead and
stainless steel). Effect of different parameters like anode current density, catholyte concentration, temperature,
and anolyte flow rate on current efficiency was studied. At current densities of 2−2.5 A/dm2 using lead as
anode at temperature of 303−313 K and anolyte flow rate of 130 − 300 cm3/min, the current efficiency of
68 − 76% with an energy consumption of 3.0 to 3.2 kWh/kg CrO3 was achieved.
The present study provides an electrochemical process for the recovery of chromium value from the solid
residue of a chromium plant using electrogenerated hypochlorite. The process was studied using an in situ
extraction method. The effect of various parameterssuch as pH, concentration of hypochlorite, particle size
of the solid effluent, pretreatment of sludge, choice of the acid for pH maintenance, and stirringon the
extraction efficiency of chromium was investigated. A significant portion (50%−60%) of the total chromium
content was recovered by performing the reaction under suitable operating conditions with hypochlorite.
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