PTMS LITHIUM COBALT ACID MATERIAL MAGNETIC Before the iron removal process, the aggregation effect of iron and aluminum slag is good, which is manifested in the large particles and loose structure, which is easy to clean the precipitation slag. And in the process of precipitation, it can prevent nickel, cobalt and other valuable components from entering the iron and aluminum slag to the greatest extent. Using this method, the immersion solution was compared with the purification solution, and the iron removal rate is 95% and the aluminum removal rate is 90%, without the secondary depth of aluminum removal.
If sodium carbonate is used for precipitation before the PTMS LITHIUM COBALT ACID MATERIAL MAGNETIC iron removal process, the iron removal rate of the leaching solution is 99% and the aluminum removal rate is 96%. After the leaching reaction breaks the waste ternary lithium ion battery, sulfuric acid and hydrogen peroxide are added to it. After stirring the reaction, the leaching liquid is obtained. The pH value of the leaching solution is 0.5~1.5.
PTMS LITHIUM COBALT ACID MATERIAL MAGNETIC Before the iron removal process, aqueous solution of sodium hydroxide is used for the copper removal reaction, the pH value of the immersion solution is adjusted to 2.5, then the immersion solution is heated to 50℃, and then the iron powder of 100~500 is added. The actual amount of iron powder was 1.2 times that of the theoretical amount. It was filtered for 4h to obtain crude copper powder and copper removal solution.
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