Treatment method of zinc-containing and iron-containing waste acid
A processing method and technology for iron powder, applied in the field of processing zinc-containing iron-containing waste acid, can solve the problems of difficulty in recycling, low recovery rate of zinc and iron, etc.
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Embodiment 1
[0071] Add 1kg of iron powder to 50kg of zinc-containing iron-containing waste acid and let it stand for 36 hours to obtain a reducing solution. The mass percentage of zinc ions in the reducing solution is 1.65%, the mass percentage of ferrous ions is 8.13%, and the mass percentage of hydrochloric acid is 0.55%.
[0072] The reducing liquid is subjected to pressure filtration treatment, and the first filtrate is collected.
[0073] Put the first filtrate into the evaporator, slowly add 7.5kg 98% concentrated sulfuric acid under stirring conditions, and obtain a mixed solution after stirring evenly.
[0074] The evaporator was evacuated, the circulating cooling water was turned on, the temperature of the evaporator was raised to 90°C, and the vacuum evaporation was concentrated for 1 hour to obtain a concentrated solution. The mass ratio of concentrated liquid to mixed liquid is 70:100. The concentrated liquid is centrifuged and filtered, and the solid obtained is a mixture of ferro...
Embodiment 2
[0076] Add 2.5 kg of iron powder to 50 kg of zinc-containing and iron-containing waste acid, and let it stand for 24 hours to obtain a reducing solution. Table 3 shows the mass percentages of zinc ions, ferrous ions, and hydrochloric acid in the untreated zinc-containing iron-containing waste acid and the reducing solution.
[0077] table 3
[0078]
[0079] The reducing liquid is subjected to pressure filtration treatment, and the first filtrate is collected. Add the first filtrate to the evaporator, slowly add 15kg of 65% concentrated sulfuric acid under stirring conditions, and obtain a mixed solution after stirring evenly.
[0080] Apply a vacuum to maintain the pressure of the evaporator at -0.095MPa, turn on the circulating cooling water, raise the temperature of the evaporator to 95°C, and concentrate by vacuum evaporation for 1.5 hours to obtain a concentrated solution. The mass ratio of concentrated liquid to mixed liquid is 64:100. Centrifugal filtration of the concentra...
Embodiment 3
[0084] Add 2.5 kg of zinc powder to 50 kg of zinc-containing iron-containing waste acid, and let it stand for 12 hours to obtain a reducing solution. The reducing liquid is subjected to pressure filtration treatment, and the first filtrate is collected. Put the first filtrate into the evaporator, slowly add 7.5kg 98% concentrated sulfuric acid under stirring conditions, and obtain a mixed solution after stirring evenly.
[0085] Apply a vacuum to maintain the pressure of the evaporator at -0.095MPa, turn on the circulating cooling water, raise the evaporator to 100°C, and concentrate by vacuum evaporation for 1.5 hours to obtain a concentrated solution. The mass ratio of concentrated liquid to mixed liquid is 64:100. The concentrated solution is spray-dried to obtain a mixture of ferrous sulfate monohydrate and zinc sulfate monohydrate, wherein the mass percentage of ferrous ions is 23.5% and the mass percentage of zinc ions is 7.05%.
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