Method for deeply removing copper from nickle electrolysis anode solution by using ion exchange resin
An ion exchange resin, nickel electrolysis technology, applied in the direction of electrolysis process, electrolysis components, improvement of process efficiency, etc., can solve problems such as inability to meet industrial application requirements, unsuitable copper, etc., achieve significant economic benefits and environmental protection value, and remove copper. The effect of high depth and avoiding the formation of copper slag
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Embodiment 1
[0036] The composition of nickel electrolysis anolyte in a factory is Ni 70.3g / L, Cu 545mg / L, Cl 85.9g / L, the pH of the feed solution is adjusted to 2.5 with hydrochloric acid, and the copper removal is carried out by ion exchange with Guangguang resin D850. The resin was metered according to the saturated adsorption capacity of Cu of the resin, and three-stage countercurrent static adsorption was carried out in the stirred tank. The adsorption temperature was 60°C, and the adsorption time of each stage was 2h. After the absorption, the Cu concentration in the liquid dropped to 35.2mg / L. The loaded resin was rinsed with a hydrochloric acid solution of pH=1.0 to elute the entrained Ni, and then desorbed with 2 mol / L hydrochloric acid, and Cu / Ni=26.4 in the desorption solution. After static adsorption, the suction liquid is pumped into the ion exchange column filled with D850 resin for deep removal of Cu. The nickel electrolyte passed through the exchange column at a flow rate o...
Embodiment 2
[0038] The composition of nickel electrolysis anolyte in a factory is Ni 85.0g / L, Cu 793mg / L, Cl 105.3g / L, the pH of the feed solution is adjusted to 3.0 with hydrochloric acid, and the copper removal is carried out by ion exchange with Guangguang resin D850. The resin was metered according to the saturated adsorption capacity of Cu of the resin, and four-stage countercurrent static adsorption was carried out in a stirred tank. The adsorption temperature was 45°C, and the adsorption time of each stage was 2h. After the absorption, the Cu concentration in the liquid dropped to 37.1mg / L. The loaded resin was rinsed with a hydrochloric acid solution of pH=1.5 to elute the entrained Ni, and then desorbed with 1 mol / L sulfuric acid, and Cu / Ni=27.9 in the desorbed solution. After static adsorption, the suction liquid is pumped into the ion exchange column filled with D850 resin for deep removal of Cu. The nickel electrolyte passed through the exchange column at a flow rate of 5 time...
Embodiment 3
[0040] The composition of nickel electrolysis anolyte in a factory is Ni 45.1g / L, Cu 217mg / L, Cl 56.2g / L, the pH of the feed solution is adjusted to 4.0 with sulfuric acid, and the copper removal is carried out by ion exchange with Guangguang resin D850. The resin was metered according to the saturated adsorption capacity of Cu of the resin, and three-stage countercurrent static adsorption was carried out in the stirred tank. The adsorption temperature was 55°C, and the adsorption time of each stage was 1.5h. After the absorption, the Cu concentration in the liquid dropped to 23.5mg / L. The loaded resin was rinsed with a hydrochloric acid solution of pH=1.5 to elute the entrained Ni, and then desorbed with 3 mol / L hydrochloric acid, and Cu / Ni=20.3 in the desorption solution. After static adsorption, the suction liquid is pumped into the ion exchange column filled with D850 resin for deep removal of Cu. The nickel electrolyte passed through the exchange column equipped with D850...
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