An optimized method for zinc recovery from electrogalvanizing waste
An optimization method and waste technology, applied in zinc oxide/zinc hydroxide and other directions, can solve the problems of low process cost and low zinc recovery rate, and achieve the effects of simple process, improved recovery rate and low recovery cost
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Embodiment 1
[0024] An optimization method for recycling zinc from electrogalvanizing waste, comprising the following optimization steps:
[0025] (1) Optimization of the acid leaching step: the mud cake is placed in a mixed acid solution for staged leaching treatment. The mixed acid is a mixture of hydrochloric acid, acetic acid, and sulfuric acid with a volume ratio of 3:2:3, and the leachate is measured every 20 minutes When the pH value increases by 1, re-add the mixed acid to the initial pH, do not continue to add the mixed acid after leaching for 2 hours, take out the filtrate, filter and save it when the pH end point is 5.0, and discard the filter residue;
[0026] (2) Optimization of evaporative concentration oxidation step: Evaporate and concentrate the filtrate obtained in step (1). When heated to 70°C, add oxidant a, maintain the temperature and continue heating for 50 minutes, then continue heating and continuous evaporative concentration operation; after heating to constant wei...
Embodiment 2
[0033] An optimization method for recycling zinc from electrogalvanizing waste, comprising the following optimization steps:
[0034] (1) Optimization of the acid leaching step: the mud cake is placed in a mixed acid solution for staged leaching treatment. The mixed acid is a mixture of hydrochloric acid, acetic acid, and sulfuric acid with a volume ratio of 3:2:3, and the leachate is measured every 20 minutes When the pH value increases by 1, re-add the mixed acid to the initial pH, do not continue to add the mixed acid after leaching for 2 hours, take out the filtrate, filter and save it when the pH end point is 5.5, and discard the filter residue;
[0035] (2) Optimization of evaporative concentration oxidation step: Evaporate and concentrate the filtrate obtained in step (1). When heated to 70°C, add oxidant a, maintain the temperature and continue heating for 60 minutes, then continue heating and continuous evaporative concentration operation; after heating to constant wei...
Embodiment 3
[0042] An optimization method for recycling zinc from electrogalvanizing waste, comprising the following optimization steps:
[0043] (1) Optimization of the acid leaching step: the mud cake is placed in a mixed acid solution for staged leaching treatment. The mixed acid is a mixture of hydrochloric acid, acetic acid, and sulfuric acid with a volume ratio of 3:2:3, and the leachate is measured every 20 minutes When the pH value increases by 1, re-add the mixed acid to the initial pH, do not continue to add the mixed acid after leaching for 2 hours, take out the filtrate, filter and save it when the pH end point is 5.2, and discard the filter residue;
[0044] (2) Optimization of evaporative concentration and oxidation step: Evaporate and concentrate the filtrate obtained in step (1). When heated to 70°C, add oxidant a, maintain the temperature and continue heating for 55 minutes, then continue heating and continuous evaporative concentration operation; after heating to constant w...
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