Method for production of zinc ingots with zero discharge of waste slag by hot dip galvanizing slag wet type smelting
A technology of hot-dip galvanizing slag and wet smelting, which is applied to the improvement of process efficiency, photography technology, instruments, etc. It can solve the problems of removing negative effects, low production technology and equipment level, increasing social costs, etc., and achieve economic benefits Significant, operable, no environmental pollution effect
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Embodiment 1
[0046] 1) Raw material treatment process: the collected hot-dip galvanizing slag is ground by a ball mill, and then the iron in the zinc material is screened out by mechanical magnetic separation to remove iron, and used as scrap iron; the ground zinc material passes through a 40-60 mesh screen Screening and filtering, the galvanized slag that has not passed the screen is used as a coarse material to be cast into a coarse zinc ingot product; some zinc oxide ash will be produced when the coarse ingot is cast, and the zinc oxide ash is mixed with the fine material to enter the primary leaching process;
[0047] 2). One-time leaching process: Add electrolyte waste to the material (zinc oxide ash, fine material under 60 mesh sieve) that enters this process in step 1). The liquid-solid mass ratio of the material to the electrolyte waste is 1.0:5.5-8.0, and the temperature is controlled. Stir and mix for 90-120 minutes at 60-80°C to leach zinc and iron in the material. The leached zinc...
Embodiment 2
[0056] The other method steps of this embodiment are the same as those of embodiment 1, and the difference is that: step 2) the liquid-to-solid mass ratio of the material in the primary leaching process to the electrolytic waste liquid is 1.0-5.0, and the stirring and mixing time is 90 minutes, The stirring and mixing temperature is: 60℃; Step 3) The electrolytic waste liquid or sulfuric acid added to the zinc slag in the secondary leaching process is subjected to secondary reaction leaching, the leaching time is 120 minutes, and the reaction temperature is 60℃; Step 4) Oxidation removal The slurry in the iron process is neutralized by adding zinc oxide to the slurry. The reaction time is 120 minutes and the reaction temperature is 65°C. In this example, from the treatment of hot-dip galvanizing slag to the production of finished zinc ingots, there is no waste residue or waste water discharge in the whole process. , No environmental pollution, remarkable economic effect.
Embodiment 3
[0058] The other method steps of this embodiment are the same as those of embodiment 1, but the difference is that step 2) The liquid-solid mass ratio of the material in the primary leaching process to the electrolytic waste liquid is 1.0-6.5, and the stirring and mixing time is 100 minutes. The temperature is 70°C; Step 3) The electrolytic waste liquid or sulfuric acid added to the zinc slag in the secondary leaching process is subjected to a secondary reaction leaching, the leaching time is 140 minutes, and the reaction temperature is 70°C; Step 4) In the oxidation iron removal process Zinc oxide is added to the slurry for neutralization reaction. The reaction time is 140 minutes and the reaction temperature is 65°C. In this example, from the treatment of hot-dip galvanizing slag to the production of finished zinc ingots, there is no waste residue, waste water discharge, and no environmental pollution. , The economic effect is remarkable.
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