Wet method smelting process of high silicon zinc oxide crude ore
A technology of hydrometallurgy and zinc oxide, which is applied in the direct leaching of high-iron zinc oxide raw ore and high-silicon field, which can solve the problems of high iron content in the solution and easy formation of silica gel, etc., so as to simplify production, reduce production cost, and broaden process technology field effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
example 1
[0016] Take zinc oxide raw ore containing 20% zinc, 20% iron, and 40% silicon, pulp it by ball milling, pulp it according to the liquid-solid ratio of zinc oxide raw ore and acid leaching solution 4:1, add acid leaching solution for leaching for 3 hours, The leaching temperature is 70°C, and 2.5% potassium permanganate and manganese dioxide by weight of the ore are added at the same time to extract the iron in the ore, and the leached pulp is neutrally concentrated by adding polyacrylamide flocculant. The supernatant is sent for purification; the concentrated underflow is used for the second-stage acid leaching operation, and the operating temperature is 60°C. The second-stage acid leaching pulp is added to the acidic pulp for acidic concentration, and the acidic supernatant is returned to the slurry. Slurry and filter residue are returned to the zinc recovery workshop. After the second-stage acid leaching pulp is filtered, there are still 3% to 6% water-soluble zinc in the ...
example 2
[0018] Take zinc oxide raw ore containing 20% zinc, 25% iron, and 45% silicon, and make pulp by ball milling. According to the liquid-solid ratio of 3:1, add acid-soluble substances for leaching for 2.5 hours at a leaching temperature of 65°C. Potassium permanganate and manganese dioxide with 3% weight of the ore will remove the iron in the ore, and the leached pulp will be concentrated by adding a neutral polyacrylamide flocculant. The concentration time is 30 minutes, and the neutral supernatant is sent to the purification operation. Concentrated bottom stream is used for second-stage acid leaching operation, operating temperature is 65°C, acidic polyacrylamide flocculant is added to the second-stage acid leaching slurry for acid concentration, the acidic supernatant is returned to the ball mill for pulping, the acidic underflow whole pulp is press-filtered, and the filtrate is sent to the ball mill for milling Slurry and filter residue are returned to the zinc recovery wor...
example 3
[0020] Take zinc oxide raw ore containing 20% zinc, 30% iron, and 50% silicon, and make pulp by ball milling. According to the liquid-solid ratio of 5:1, acid-soluble substances are added for leaching for 2 hours, and the leaching temperature is 60°C. Potassium permanganate and manganese dioxide with a weight of 3.5% of the ore will remove the iron in the ore, and the leached pulp will be concentrated by adding a neutral polyacrylamide flocculant. The concentration time is 25 minutes, and the neutral supernatant is sent to the purification operation. The concentrated underflow is carried out in the second-stage acid leaching operation. The operating temperature is 70°C. The second-stage acid leaching slurry is acid-concentrated by adding acidic polyacrylamide flocculant, and the resulting acidic supernatant is returned to the ball mill for pulping. Slurry and filter residue are returned to the zinc recovery workshop.
[0021] Below is the production contrast of high silicon ...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com