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A method for extracting Pb, In, Ag from indium-containing lead silver slag

A lead-silver slag, sponge lead technology, applied in the improvement of process efficiency, photography technology, instruments and other directions, can solve the problems of waste of resources, large equipment investment, indium can not be recovered, etc., to achieve full recovery, improve production efficiency, The effect of improving filtration performance

Inactive Publication Date: 2018-06-05
贵州省兴安环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional smelting method of lead and silver slag is pyrometallurgy. The blast furnace is used to reduce and smelt lead, and the silver is also reduced to a metal state and enters the crude lead to form a lead-silver alloy. Then the lead and silver are separated by electrolytic refining. This method can well Lead is extracted, but the recovery rate of silver is not high. Some silver and most of indium enter the slag and are difficult to recover, resulting in a waste of rare and precious metal resources. In addition, the fire method of lead smelting has great environmental pollution, high energy consumption, and the recovery rate of rare and precious metals. Secondly, most of the current production adopts the flotation method to treat the lead and silver slag, first separate and extract the silver, and then use the fire method to extract the lead. This method is ideal for the extraction of metallic lead and precious metal silver, but it is not suitable for the extraction of precious metals The lead-silver slag of indium, indium cannot be recovered well, which will cause waste of resources; there is also the use of pressure oxidation leaching, through which the sulfides such as ZnS and InS in the material can be oxidized and leached, Let the Zn and In in it be fully leached and recovered. The indium content in the leached slag is naturally low, and then the lead and silver are recovered through other methods of smelting lead and silver slag. This method is an ideal recovery method, which can make Zn and In one time However, the pressure oxidation leaching has the disadvantages of large equipment investment, high requirements for equipment and technical personnel, and it is difficult to implement and apply to small and medium-sized enterprises.

Method used

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  • A method for extracting Pb, In, Ag from indium-containing lead silver slag

Examples

Experimental program
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Effect test

Embodiment 1

[0020] A batch of raw materials containing zinc 11.28%, Pb3.51%, Fe12.47%, Si15.83%, In652g / t, Ag273g / t are reduced, oxidized, roasted and volatilized in a rotary kiln to obtain cloth bag powder, which is leached twice with sulfuric acid The indium-containing lead silver slag obtained after separating and extracting Zn and In has the following chemical composition: Pb45.04%, In356g / t, Ag279g / t, Zn 2.15%, Fe 1.14%, Si4.36%. Alkaline leaching of Pb from silver slag: take 200g of indium-containing lead silver slag, carry out alkaline leaching once according to liquid-solid ratio L / S=4, leaching solution NaOH (=250g / L, temperature 85°C, stirring time 2h; once leaching slag Then according to L / S=8, leaching solution NaOH (=250g / L, temperature 85°C, stirring time 3h, carry out leaching twice. The content of primary leaching solution (1000mL) is: Pb58.7g / L, Zn2.65g / L, In content; secondary leaching liquid (800mL) content: Pb14.3g / L, Zn1.04g / L; secondary leaching residue (81.5g) conte...

Embodiment 2

[0022] Adopt one-time alkaline immersion solution (1000mL) in embodiment 1 to carry out electrolysis Pb, electrolysis condition is: with stainless steel plate as cathode and anode plate, pole distance L=80cm, cell voltage is 1.2V, and current density is 150A / m 2 , electrolysis temperature 35 ℃, electrolysis time 8h; electrolysis sponge lead 43.2g, electrolysis raffinate containing Pb16.4g / L.

Embodiment 3

[0024] Adopt the indium-containing lead-silver slag to carry out NH earlier in the embodiment one 4 F solution is washed, and the slag is alkaline leached Pb by the condition of example 1 again, NH 4 F solution washing conditions are: liquid-solid ratio L / S=6, NH 4 The amount of F added is 10g / L, the temperature is 70°C, the stirring time is 1h, and the washing liquid contains H 2 SO 4 8.54g / L, Zn1.34g / L, In 9.6mg / L; secondary alkaline leaching residue (71.4g) content: Pb12.17%, In914g / t, Ag703g / t, Zn 1.05%; leaching rate ( Slag meter): Pb90.35%; twice alkaline leaching filtration speed is faster.

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Abstract

The invention discloses a method for extracting Pb, In and Ag from indium-containing lead silver residues. The method comprises the following steps of: Pb extracting, In extracting and Ag extracting. The method disclosed by the invention is used for sufficiently recycling resources by recycling valuable metal Pb, In and Ag from the indium-containing lead silver residues, has a very high economic value, and also avoids pollution of the lead silver residues on environment.

Description

technical field [0001] The invention relates to a method for extracting metal compounds by a wet method, in particular to a method for extracting Pb, In and Ag from lead-silver slag containing indium. Background technique [0002] Extracting valuable metals such as Zn, In, Pb, etc. from materials containing zinc, indium, lead, silver, etc. with low grades often needs to be reduced, oxidized, and roasted in a rotary kiln first, so that the valuable metals can be volatilized and enriched and combined with iron. , silicon, calcium and other elements are separated, most of the valuable metals Zn, In, Pb form oxides and enter the bag dust collection system, and then use neutral leaching-leaching solution to purify and remove impurities, then perform electrolytic separation to extract zinc, and use neutral leaching to make The indium in the slag is further enriched, and then carry out sulfuric acid leaching of In and neutral leaching of residual Zn. The acidic leaching solution is...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/04C22B13/00C22B58/00C22B11/00C25C1/18
CPCC22B7/04C22B11/042C22B13/045C22B58/00C25C1/18Y02P10/20
Inventor 曾光祥李世平周代江韦国龙王志斌
Owner 贵州省兴安环保科技有限公司