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Method for comprehensively recovering valuable metals and arsenic trioxide from copper ash and arsenic sulfide slag

A technology of arsenic trioxide and valuable metals, applied in arsenic oxide/arsenic hydroxide/oxyacid arsenic, chemical instruments and methods, arsenic compounds, etc., can solve problems such as poisoning

Pending Publication Date: 2021-11-19
CINF ENG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are mainly three processes of water leaching, acid leaching and alkali leaching in wet separation. CN105567983A discloses a water leaching-alkali leaching treatment process for copper smelting dust, which separates arsenic from metal, and the prepared arsenic products are not marketable; CN104357668A publishes A method of leaching smoke dust with dirty acid and removing arsenic by electrodeposition, however, arsine hydrogen is easily produced in the process of acid leaching and electrodeposition to cause poisoning; CN201210534763.5 discloses a multi-metal comprehensive recovery process for copper smelting soot , part of the chemical reagent sodium sulfide needs to be added in the process, and the product arsenic trioxide does not indicate whether it meets the national standard GB-26721-2011 for arsenic trioxide

Method used

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  • Method for comprehensively recovering valuable metals and arsenic trioxide from copper ash and arsenic sulfide slag

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Embodiment 1

[0022] The accompanying drawings of this embodiment are shown in figure 1 .

[0023] The chemical composition of the main elements in the copper fume and arsenic sulfide slag described in the present invention is shown in the table below:

[0024] Cu As Zn Pb Bi S copper soot 4.85% 12.10% 15.26% 18.41% 2.26% 10.39% Arsenic sulfide slag 0.15% 52.97% 0.18% —— —— 37.32%

[0025] Copper soot 1kg, first use 60g / L sulfuric acid for the first stage leaching, the leaching liquid-solid ratio is 4:1mL / g, the leaching time is 2.0h, and the leaching temperature is 75°C. After filtration, 3.625L of acid leaching liquid and acid leaching residue are obtained 595.3g (wet weight); the acid leaching slag was leached in the second stage with industrial water, the leaching liquid-solid ratio was 2:1mL / g, the leaching time was 1.0h, and the leaching temperature was 75°C. After filtration, 1.075L of water leaching liquid and lead Bismuth slag 547.73...

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Abstract

The invention discloses a method for comprehensively recovering valuable metals and arsenic trioxide from copper ash and arsenic sulfide slag. The method comprises the following steps that (1) two-stage leaching is performed on the copper ash; (2) second-stage copper deposition is performed by the aid of the arsenic sulfide slag; (3) SO2 is used for reduction and arsenic removal; and (4) evaporative crystallization is performed. According to the method, the valuable metals and the arsenic trioxide are comprehensively recovered through interaction of components in the two different kinds of waste, namely the copper ash and the arsenic sulfide slag. The method specifically comprises the steps that two-stage leaching is adopted, valuable metals copper, zinc, arsenic and the like in the copper ash enter a solution, metals such as lead, bismuth and the like enter slag, and lead-bismuth slag can serve as a raw material for lead smelting; the acid leaching solution adopts arsenic sulfide slag for two-stage copper deposition, so that copper sulfide with low arsenic content is obtained, and meanwhile, a part of hazardous waste arsenic sulfide slag is also utilized; the percentage content of As2O3 in refined As2O3 obtained after SO2 is added into the copper deposition liquid for reduction and arsenic removal is larger than 95%; the content of copper in refined zinc sulfate heptahydrate obtained by evaporative crystallization of the arsenic-removed zinc liquid is less than 0.05%, and the content of arsenic is less than 2%.

Description

technical field [0001] The invention relates to comprehensive recovery of metal copper, zinc, lead, bismuth and arsenic, in particular to a method for comprehensive recovery of valuable metals and preparation of arsenic trioxide from copper soot and arsenic sulfide slag. [0002] technical background [0003] The raw material for copper smelting is mainly copper sulfide concentrate, which contains a certain amount of arsenic. In the process of pyrometallurgy, a large amount of arsenic in copper sulfide concentrate will volatilize into the flue gas, and then into the copper fume and waste acid. In addition, in addition to arsenic, soot also contains a large amount of valuable metals such as copper, lead, zinc, bismuth, gold, silver, etc. Therefore, the harmless and resourceful utilization of copper soot has always been the focus of enterprises. After the arsenic in the flue gas enters the purified waste acid, it will first go through the sulfidation process, and then enter th...

Claims

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Application Information

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IPC IPC(8): C22B7/02C22B7/04C22B30/04C22B19/30C22B19/20C22B15/00C22B13/00C01G28/00C01G9/06
CPCC22B7/02C22B7/04C22B7/007C22B30/04C22B19/30C22B19/22C22B19/26C22B15/0071C22B15/0089C22B13/045C01G28/005C01G9/06Y02P10/20
Inventor 杨建平张乐如谢冰包洪光郭徽
Owner CINF ENG CO LTD
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