铜镍电镀退镀废液资源化处理工艺

针对硝酸型铜镍退镀废液,确定了蒸馏法回收硝酸、溶剂萃取法分离提取铜、沉淀分离法回收镍的工艺路线.探讨了采用P507煤油体系萃取分离硝酸介质中的铜和镍及用硫酸反萃铜的条件及影响规律,确定了最佳工艺参数.结果表明,硝酸回收率可达97.8%;当最佳萃取工艺条件为:料液浓度Cu 15～20mg/mL,Ni 5～10 mg/mL,料液pH为1～2,萃取剂体积分数35%,皂化度60%,相比为1∶1,振荡时间2min,温度20℃～25℃,铜的一级萃取率达90%以上,铜镍分离系数为75,经过三级逆流萃取废液中的铜镍已达到完全分离;以NaOH作沉淀剂,溶液的pH为10～11,镍的回收率可达99.9%.经上述处理后,使排放液达到国家工业废水排放标准要求.

Recovery Process of Nitric Acid, Copper and Nickel in Deplating Wastewater

The recovery process of nitric acid, copper and nickel in deplating wastewater was developed by using the combined technique of distillation, solvent extraction and precipitation. The conditions of the separation of copper and nickel by solvent extraction using P507 in kerosene and stripping copper with H2SO4 were specially investigated and the optimal parameters were determined. The results of experiment indicated that the recovery ratio of nitric acid was 97.8%, and under the optimized conditions of extraction process, concentration of original effluence ranged in 15-20 mg/mL copper, 5-10 mg/mL nickel, pH 1-2, concentration of extractant was 35% (V/V), saponification degree was 60%, phase ratio was 1:1, reaction time was 2 min, temperature ranged in 20 degrees C-25 degrees C, the one stage extraction efficiency of copper was higher than 90%, the separation ratio of copper and nickel was up to 75; copper and nickel could be completely separated by a continuous countercurrent three-stage extraction. The nickel could be recovered from the water phase by precipitating with NaOH and the recovery ratio of nickel reached up to 99.9% by controlling pH in solution within 10-11. After these treatment, the effluent could meet the national standards of wastewater discharge.