This technology improves the separation factor between Co and Cu and reduces the number of stages in the refining process by inducing a synergistic effect. This is achieved by mixing D2EHPA solvent with PC88A or Cyanex 272 in a specific ratio during the impurity removal stage of the spent battery hydrometallurgical process.
In the process of recovering valuable metals (Ni, Co, Li) from spent batteries, the difficulty in separating specific impurities, particularly copper (Cu), has led to an increase in the number of washing stages and higher overall process costs.
By using an organic solvent based on D2EHPA mixed with PC88A or Cyanex 272 in a ratio of 1:1 to 3:1 (preferably 2:1) to remove impurities at a pH of 2.0 to 3.0, this technology can substantially contribute to securing commercial competitiveness in resource circulation and recycling.
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