Electrocobalt production method capable of recycling by-products
A production method and technology of by-products, applied in the field of electric cobalt production, can solve problems such as dangerous sources, prone to combustion and explosion, sodium chlorate production and transportation restrictions, and achieve the effect of solving supply problems and solving open circuit problems
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Embodiment 1
[0014] A method for producing electric cobalt with recyclable by-products, comprising the following steps: acid-dissolving an intermediate product of cobalt hydroxide, wherein the mass fraction of metal elements in the intermediate product of cobalt hydroxide is 30% for cobalt and 0.3% for copper. %, the manganese content is 1.8%, the nickel content is 0.06%, the iron content is 0.007%, the calcium content is 0.3%, the zinc content is 0.15%, and other impurities are acid-dissolved with hydrochloric acid, and the pH value is 1.0, and then removed Impurities and enrichment, specifically using chemical precipitation to remove iron, P204 to remove calcium, copper, zinc and manganese, 507 to remove nickel, and then continuous electrowinning, the reaction tank voltage is 2.8V, the current is 1A, and the temperature is 50°C. Cobalt flakes and chlorine gas are obtained after electrowinning , mix chlorine gas with liquid caustic soda, control the temperature of liquid caustic soda at 70...
Embodiment 2
[0017] A method for producing electric cobalt with recyclable by-products, comprising the following steps: acid-dissolving an intermediate cobalt hydroxide, wherein the mass fraction of metal elements in the intermediate cobalt hydroxide is 40% cobalt and 1.7% copper. %, the manganese content is 4%, the nickel content is 0.5%, the iron content is 0.09%, the calcium content is 0.7%, the zinc content is 0.25%, and other impurities are acid-dissolved with sulfuric acid, and the pH value is 1.5, and then removed Miscellaneous, enrichment, and then adopt continuous electrowinning, the reaction tank voltage is 3.5V, the current is 9000A, and the temperature is 70°C. After electrowinning, cobalt flakes and chlorine gas are obtained. The chlorine gas is mixed with liquid caustic soda, and the temperature of the liquid caustic soda is controlled at 75°C. The resulting mixed solution of sodium chlorate and sodium chloride returns to the acid solution together to achieve coarse impurity r...
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