Industrial waste nitric acid comprehensive utilization process
A waste nitric acid, industrial technology, applied in the directions of nitric acid, nitrogen oxides/oxyacids, copper oxide/copper hydroxide, etc., can solve the problems of interfering with resource recovery to be studied, high operating costs, complex processes, etc., to avoid The effect of secondary pollution, easy operation and reducing the amount of alkali
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Embodiment 1
[0030] Treatment of nitric acid-type tin stripping solution. The nitric acid-type tin stripping solution is mainly composed of ferric nitrate and nitric acid. The acid concentration reaches about 20-25%. A large amount of waste liquid will be produced, and the waste tin stripping liquid is one of the largest waste liquids, which contains a large amount of acid, tin, copper, etc.
[0031] Take nitric acid type tin stripping solution 1m 3 , add 100kg of copper-containing waste, keep warm at 70°C, stir and leaching, detect the copper content in the leaching solution, when the mass percentage concentration of copper content in the leaching solution reaches 9%, add copper hydroxide to purify the leaching solution, and adjust the solution. pH value=4, stirred for 0.5h to remove Sn and Fe impurities in the solution; press filter, and the filter residue was sold as a material containing Sn and Fe; the filtrate was concentrated by evaporation, and the evaporated concentrate was placed ...
Embodiment 2
[0033] Treatment of waste nitric acid stripping solution, the waste nitric acid stripping solution is mainly composed of HNO 3 , Cu(NO 3 ) 2 Composition, the concentration of acid reaches about 20%, and Ni ions are precipitated between P=4-5.
[0034] Take waste nitric acid strip solution 1m 3 , add 120kg of copper-containing waste, keep warm at 60-80°C, stir and leaching, detect the copper content in the leaching solution, when the mass percentage concentration of copper content in the leaching solution reaches 8%, add copper hydroxide to purify the leaching solution, adjust The pH value in the solution is 3.5, stir for 0.5h to remove the Fe impurities in the solution; press filter, and the filter residue is sold as Fe-containing material; the filtrate is concentrated by evaporation, and the evaporated concentrate is cooled at 15°C for 2h, crystallization occurs Copper nitrate, while the mother liquor is returned to heating and leaching; the steam generated by evaporation ...
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