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Process for recovering bismuth from bismuth slag

A process method and technology for bismuth slag are applied in the field of recovering bismuth from bismuth slag, which can solve the problems of waste of resources and environment, repeated smelting, complex properties of slag in the later stage, etc., and achieve the effects of low energy consumption, simple operation and high recovery rate.

Inactive Publication Date: 2020-02-14
四川正祥环保技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Most smelters in China store the slag in the later stage for further processing or sell it as an intermediate product at a low price. At present, there are two traditional processing methods: fire method and wet method, reverberatory furnace and converter smelting, both of which tend to be single element or precious metals such as gold and silver. Recycling and extraction, so that other valuable metal elements cannot be completely recovered, resulting in waste of resources and environmental pollution
The properties of later-stage slag are complex, and the treatment methods of later-stage slag with different components are also different. For later-stage slag containing more rare and precious metals, gold and silver are concentrated and recovered through leaching; for late-stage slag with high heavy metal content, lead and copper are mainly recovered. Traditional The treatment method can only selectively recover metals, and cannot recover more valuable metals in the same process, which is likely to cause repeated smelting

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] A, 15t of bismuth slag (Bi 16.0wt%, Cu 5.0wt%, Ag 0.9wt%) is dropped into a jaw crusher and crushed to a particle size of 5mm, and ground to 120 mesh in a ball mill to obtain bismuth slag powder for subsequent use;

[0034] B, add water 84t, sulfuric acid 16t and industrial salt 10t and mix successively in reaction inner tank, obtain leachate;

[0035] C. Heat the leaching liquid obtained in step B to 70°C by steam heating, then add 22t of bismuth slag powder obtained in step A, and leaching and reacting at 80°C for 2 hours, the pH value is controlled at 0.5, and the leaching is observed every 30 minutes, and the tank is opened Cover the surface feeding port, scoop out the leaching residue in the tank with a water ladle to observe the color of the solution, when the leaching residue all turns grayish white, filter the leaching solution to obtain the first filtrate;

[0036] D, in the first filtrate that step C obtains, add soda ash pH value and reach 1.5, then add water...

Embodiment 2

[0042] A. Put 15t of bismuth slag (Bi 16.0wt%, Cu 5.0wt%, Ag 0.9wt%) into a jaw crusher and crush it to a particle size of 4mm, and grind it to 120 mesh in a ball mill to obtain bismuth slag powder for subsequent use;

[0043] B, add water 82t, sulfuric acid 18t and industrial salt 10t and mix successively in reaction inner tank, obtain leachate;

[0044] C. Heat the leaching solution obtained in step B to 70°C by steam heating, then add 22t of bismuth slag powder obtained in step A, and leaching and reacting at 85°C for 2 hours, the pH value is controlled at 0.8, and the leaching is observed every 30 minutes, and the tank is opened Cover the surface feeding port, scoop out the leaching residue in the tank with a water ladle to observe the color of the solution, when the leaching residue all turns grayish white, filter the leaching solution to obtain the first filtrate;

[0045] D, in the first filtrate that step C obtains, add soda ash pH value and reach 1.5, then add water c...

Embodiment 3

[0051] A. Put 15t of bismuth slag (Bi 16.0wt%, Cu 5.0wt%, Ag 0.9wt%) into a jaw crusher and crush it to a particle size of 3mm, and grind it to 120 mesh in a ball mill to obtain bismuth slag powder, which is set aside;

[0052] B, add water 81t, sulfuric acid 19t and industrial salt 10t and mix successively in reaction inner tank, obtain leachate;

[0053] C. Heat the leaching solution obtained in step B to 70°C by steam heating, then add 22t of bismuth slag powder obtained in step A, and leaching and reacting at 90°C for 2 hours, the pH value is controlled at 1, the leaching is observed every 30 minutes, and the tank is opened Cover the surface feeding port, scoop out the leaching residue in the tank with a water ladle to observe the color of the solution, when the leaching residue all turns grayish white, filter the leaching solution to obtain the first filtrate;

[0054] D, in the first filtrate that step C obtains, add soda ash pH value and reach 1.5, then add water contro...

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PUM

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Abstract

The invention belongs to the field of bismuth refining, and in particular, relates to a process for recovering bismuth from bismuth slag. Later slag (bismuth slag) of a dore furnace is crushed to feedin a ball mill to mill as powder; then, the powder is fed in a leaching tank with sulfuric acid, industrial salt and water solution for reaction by a period of time at a temperature of 80-90 DEG C; bismuth and copper are fed in the solution; and leaching liquid realizes liquid-solid separation through a plate frame filter press. Through neutralization, hydrolytic bismuth is precipitated in a slagform; copper in the solution is replaced by iron powder to finally prepare sponge copper; the bismuth slag is smelted by a pyrogenic reduction furnace to prepare crude bismuth; and the crude bismuthis refined and purified to obtain final products-refined bismuth. The process is convenient to operate, high in recovery rate of bismuth and low in energy consumption, and solves the difficulties of single recovered element, longer flow and low metal recovery rate in a traditional dore furnace later slag treatment method.

Description

technical field [0001] The invention belongs to the field of bismuth refining, in particular to a process for recovering bismuth from bismuth slag. Background technique [0002] With the continuous development of non-ferrous smelting, easy-to-handle minerals and raw materials are increasingly reduced and exhausted. Various difficult-to-handle ores and complex materials of valuable metals, such as waste generated during the smelting process, production by-product materials, etc., have gradually become valuable metal elements. recycled secondary resources. The late slag of the silver separation furnace is the late slag with complex composition obtained after the lead anode slime is smelted and blown for silver separation. It has become a valuable raw material for comprehensive recovery because it contains bismuth, lead, silver, antimony and other metals. [0003] Most smelters in China store the slag in the later stage for further processing or sell it as an intermediate prod...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B30/06C22B7/04C22B15/00
CPCC22B7/001C22B7/007C22B7/04C22B15/0071C22B15/0091C22B30/06Y02P10/20
Inventor 巫文嵩程辉
Owner 四川正祥环保技术有限公司