[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.
Liu
Zhenhai
Z
Department of Environmental Science and Engineering, Harbin Institute of Technology, Harbin 150001, China.
Wang
Peng
P
Jiang
Hongquan
H
Chen
Zhichuan
Z
D003300:Copper / Q000302:isolation & purification*; D006863:Hydrogen-Ion Concentration; D007220:Industrial Waste; D009532:Nickel / Q000302:isolation & purification*; D017942:Nitric Acid / Q000302:isolation & purification*; D014865:Waste Disposal, Fluid
D007220:Industrial Waste; D017942:Nitric Acid; D003300:Copper; D009532:Nickel