Systems and methods of cleaning cabin air in a transportation vehicle
US-2016288043-A1 · Oct 6, 2016 · US
US2020332390A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020332390-A1 |
| Application number | US-202016822141-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 18, 2020 |
| Priority date | Apr 16, 2019 |
| Publication date | Oct 22, 2020 |
| Grant date | — |
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The present invention discloses a method for preparing iron ore concentrates by recycling copper smelting slag tailings, and belongs to the technical field of metallurgy and tailings recycling. In the present invention, copper slag tailings obtained after copper pyrometallurgy and flotation and water are used as raw materials, and low-concentration sulfur dioxide flue gas is used as a leaching agent for leaching of metals such as iron, zinc, copper, arsenic, and silicon in the slag tailings; the leachate is purified step by step through processes such as replacement by metal iron powder and sulfide precipitation control, to separate zinc, copper, arsenic, etc.; a purified solution is mainly composed of FeSO4 or can be used for producing a ferric salt flocculant; obtained tailings are used to obtain iron ore concentrates through magnetic separation, and the obtained iron ore concentrates can be used for further producing ultra-pure iron ore concentrates.
Opening claim text (preview).
1 . A method for preparing iron ore concentrates by recycling copper slag tailings, comprising the following steps: (1) purifying and absorbing SO 2 flue gas with a SO 2 concentration of 100-1000 mg/m 3 by using copper slag tailings slurry, discharging the slurry when a concentration of SO 2 at a flue gas outlet is greater than 100 mg/m 3 , and conducting filtering; (2) adding iron powder to the filtrate under stirring at room temperature to 80° C., wherein an addition amount of the iron powder is 2-5 times of a theoretical amount thereof for replacement of Cu 2+ and Fe 3+ ; conducting replacement reaction for 30-120 min; and conducting solid-liquid separation, to obtain copper-containing slag and replacement liquid; (3) adding a sulfiding agent to the replacement liquid for precipitation of zinc and arsenic ions, to obtain zinc-containing slag and iron-containing slurry, wherein an addition amount of the sulfiding agent is 3-8 times of a theoretical amount thereof for precipitation of the zinc and arsenic ions; and (4) placing the filter residue obtained in step (1) in a wet magnetic separation device, conducting magnetic separation in a magnetic field with intensity of 0.05-0.2 T to obtain rough iron ore concentrates and tailings, returning the tailings along an original route of a slag dump for treatment, and further conducting magnetic separation on the rough iron ore concentrates to obtain iron ore concentrates. 2 . The method for preparing iron ore concentrates by recycling copper slag tailings according to claim 1 , wherein the volume content of O 2 in the SO 2 flue gas is 12-21%, and the flue gas temperature is 20-100° C. 3 . The method for preparing iron ore concentrates by recycling copper slag tailings according to claim 1 , wherein a solid-to-liquid ratio of copper slag tailings to water in the copper slag tailings slurry is 1:3-1:8. 4 . The method for preparing iron ore concentrates by recycling copper slag tailings according to claim 1 , wherein a particle size of the iron powder is 45-100 μm, and the mass content of iron in the iron powder is greater than 98%. 5 . The method for preparing iron ore concentrates by recycling copper slag tailings according to claim 1 , wherein the sulfiding agent is ferrous sulfide or sodium sulfide, and a particle size of the ferrous sulfide is 37-150 μm.
Sulfur oxides (B01D53/60 takes precedence) · CPC title
Removing sulfur, phosphorus or arsenic other than by roasting · CPC title
by cementation · CPC title
Inorganic bases or salts · CPC title
containing sulfur · CPC title
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