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Method for pretreating indium-containing zinc oxide acid supernatant

A zinc oxide and pretreatment technology, applied in the direction of improving process efficiency, etc., can solve the problems of high impurity content and inability to carry out extraction, and achieve the effects of improving indium recovery rate, simplifying indium recovery process, and reducing consumption

Active Publication Date: 2014-08-27
ZHUZHOU SMELTER GRP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] The invention solves the technical problem that the high impurity content in the direct extraction of the indium-containing zinc oxide supernatant in the prior art leads to the inability to carry out the extraction, and provides a pretreatment method for the indium-containing zinc oxide supernatant

Method used

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  • Method for pretreating indium-containing zinc oxide acid supernatant

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] The composition of the indium-containing zinc oxide supernatant of the present invention is: In 3+ 0.92g / L, Bi 3+ 0.12g / L, Sn 2+ 0.11g / L, SiO 2 0.36g / L, Fe 2+ 20.83g / L, Fe 3+ 23.71g / L, Cu 2+ 0.73g / L, Zn 2+ 87.36g / L, As 3+ 1.59g / L, Cl - 0.89g / L,H 2 SO 4 71.53g / L.

[0045] Step 1: Reduction: Add the zinc sulfide concentrate after ball milling to the constantly stirring indium-containing zinc oxide supernatant, and the addition amount of the zinc sulfide concentrate is Fe 3+ All reduced to Fe 2+ The theoretical dosage is 1.0 times, the reduction temperature is 95°C, and the time is 2 hours. After filtration, the reduction solution and reduction slag are obtained, and the reduction slag returns to the zinc system to recover zinc. The main components of the reducing solution are: In 3+ 0.91g / L, Fe 2+ 40.15g / L, Fe 3+ 4.78g / L, Zn 2+ 98.35g / L, Bi 3+ 0.13g / L, Sn 2+ 0.11g / L, SiO 2 0.34g / L, Cu 2+ 0.78g / L, As 3+ 1.51g / L, Cl - 0.93g / L,H 2 SO ...

Embodiment 2

[0051] The composition of the supernatant containing indium zinc oxide acid of the present embodiment is: In 3+ 0.92g / L, Bi 3+ 0.12g / L, Sn 2+ 0.11g / L, SiO 2 0.36g / L, Fe 2+ 20.83g / L, Fe 3+ 23.71g / L, Cu 2+ 0.73g / L, Zn 2+ 87.36g / L, As 3+ 1.59g / L, Cl - 0.89g / L,H 2 SO 4 71.53g / L.

[0052] Step 1: Reduction: Add the zinc sulfide concentrate after ball milling to the constantly stirring indium-containing zinc oxide supernatant, and the addition amount of the zinc sulfide concentrate is Fe 3+ All reduced to Fe 2+ The theoretical dosage is 1.2 times, the reduction temperature is 85°C, and the time is 3.5 hours. After filtration, the reduction solution and reduction residue are obtained, and the reduction residue zinc return system recovers zinc. The main components of the reducing solution are: In 3+ 0.91g / L, Fe 2+ 41.08g / L, Fe 3+ 3.92g / L, Zn 2+ 99.15g / L, Bi 3+ 0.13g / L, Sn 2+ 0.12g / L, SiO 2 0.38g / L, Cu 2+ 0.81g / L, As 3+ 1.65g / L, Cl - 0.97g / L,H ...

Embodiment 3

[0058] The composition of the supernatant containing indium zinc oxide acid of the present embodiment is: In 3+ 0.92g / L, Bi 3+ 0.12g / L, Sn 2+ 0.11g / L, SiO 2 0.36g / L, Fe 2+ 20.83g / L, Fe 3+ 23.71g / L, Cu 2+ 0.73g / L, Zn 2+ 87.36g / L, As 3+ 1.59g / L, Cl - 0.89g / L,H 2 SO 4 71.53g / L.

[0059] Step 1: Reduction: Add the zinc sulfide concentrate after ball milling to the constantly stirring indium-containing zinc oxide supernatant, and the addition amount of the zinc sulfide concentrate is Fe 3+ All reduced to Fe 2+ The theoretical dosage is 1.3 times, the reduction temperature is 75°C, and the time is 5 hours. After filtration, the reduction solution and reduction slag are obtained, and the reduction slag returns to the zinc system to recover zinc. The main components of the reducing solution are: In 3+ 0.90g / L,Fe 2+ 41.54g / L, Fe 3+ 3.16g / L, Zn 2+ 99.83g / L, Bi 3+ 0.14g / L, Sn 2+ 0.13g / L, SiO 2 0.41g / L, Cu 2+ 0.91g / L, As 3+ 1.64g / L, Cl - 0.98g / L,H ...

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Abstract

The invention provides a pretreatment method for the supernatant of zinc oxide zinc oxide containing indium, comprising the following steps: A. Reduction: adding the zinc sulfide concentrate after ball milling to the supernatant of zinc oxide zinc oxide containing indium, and filtering to obtain the reducing solution after reaction B, purification: add iron powder to the reducing solution, and qualitatively detect that Fe3+ content in the solution is qualified to obtain a purification solution; C, desiliconization: add bone glue to the purification solution to obtain a desiliconization solution; D, deoiling: remove Add a deoiling agent to the silicon liquid to obtain a deoiling liquid; E, adjust acid zinc and filter: add sulfuric acid and water to the deoiling liquid until the acidity and zinc ion concentration of the system meet the extraction requirements, then filter to obtain a pretreatment liquid and Pretreatment slag. The pretreatment method of the indium-containing zinc oxide supernatant provided by the present invention can remove impurities that affect indium extraction in the indium-containing zinc oxide supernatant, and obtain a pre-extraction liquid suitable for direct extraction of indium, and simultaneously bismuth, copper , tin and other valuable metals to achieve enrichment.

Description

technical field [0001] The invention relates to a method for comprehensively recovering indium from zinc oxide in a wet zinc smelting process, in particular to a pretreatment method for indium-containing zinc oxide supernatant. Background technique [0002] Generally speaking, in the existing zinc hydrometallurgy process, there are two main processes for recovering indium from zinc oxide by wet method: one is to directly leaching zinc oxide with low-acid to enrich indium from the low-acid leaching solution, Generate enriched slag, and then use alkali boiling→acid dissolution→replacement→melting and casting to obtain crude indium, and electrolysis of crude indium to obtain refined indium. This process has the disadvantages of long process, high labor intensity, high unit production cost and low indium recovery rate. The other method is neutral leaching of indium-containing zinc oxide (neutral leaching means that the pH value of the leaching end point is around 5.0, hereinafte...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/24C22B3/44C22B19/00C22B58/00
CPCY02P10/20
Inventor 刘一宁廖贻鹏刘敏窦传龙周正军王文录王荣辉
Owner ZHUZHOU SMELTER GRP