Method for efficiently separating copper arsenic in arsenic matte

An arsenic matte, high-efficiency technology, applied in the field of efficient separation of copper and arsenic from arsenic matte, can solve the problems of high operating cost, low metal recovery rate, long process flow, etc., and achieve high recovery rate of valuable metals, good copper and arsenic The effect of separation and short process flow

Inactive Publication Date: 2019-01-04
CHENZHOU FENGYUE ENVIRONMENTAL PROTECTION TECH
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Problems solved by technology

The main process of pyroprocessing is to blow smelting matte copper to obtain blister copper, and then further refining to obtain refined copper. However, the pyroprocessing process has serious problems such as large environmental pollution, long process flow, high operating cost and low metal recovery rate.
In order to make up for these deficiencies, researchers turned their attention to the wet treatment process. At present, there are two schemes for wet treatment, acid leaching and alkali leaching. For example, the 2011 Chinese Invention Patent Publication No. CN201110191860. 3 -(NH 4 ) 2 SO 4 Oxygen pressure leaching of arsenic matte in a weak alkaline composite system at a temperature of 110-200 ° C, copper and NH 3 Coordination chemical reaction occurs to enter the solution to separate copper; but more is the method of using sulfuric acid acid leaching arsenic matte, such as the 2014 Chinese Invention Patent Publication No. CN201410595856.8, CN201410519503.X and the 2015 Chinese Invention Patent Publication No. CN201510252217.6 all use sulfuric acid solution to leaching arsenic matte copper, but the specific operations and conditions are different, and the content of each element in the leachate is also very different, which also directly affects the purification of the leachate and the copper electrowinning section For the treatment of copper sulfate leaching solution with high impurity content, there is currently a technology to electrolyze copper by using swirl electrolysis. This technology has relatively low requirements for arsenic content and other impurity elements in the solution, and can adapt to a wide range of copper sulfate electrolysis. Liquid is a well-developed technology at present, but for most copper electrowinning enterprises, most of them still use the traditional copper sulfate electrolysis process and equipment, and it takes several thousand dollars to build a set of swirl electrolysis equipment. 10,000, it is difficult for many small and medium-sized enterprises to afford this cost at once, and the old equipment and processes in the enterprise can be used temporarily so they will not be eliminated at once, which requires that the impurities in the copper sulfate leaching solution should be as small as possible to meet our requirements. Old copper electrowinning production line

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  • Method for efficiently separating copper arsenic in arsenic matte

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] Arsenic matte (Cu 49.22wt%, As 15.83wt%, Fe 1.75wt%, S 0.6wt%, Pb 15.69wt%, Sb 6.05wt%, Ag 3071g / t) was crushed, ground and passed through a 100-mesh sieve. Take 150g arsenic matte powder with sulfuric acid solution and Cu 2+ Ions are added to the reaction kettle, the concentration of sulfuric acid solution is 150g / L, the temperature is set at 130°C, the liquid-solid ratio is 6:1 (mL / g), the oxygen partial pressure is 0.8MPa, Cu 2+ The amount of ions added is 2g / L, and the reaction time is 4h. After the leaching reaction is completed, liquid-solid separation is carried out to obtain a copper sulfate leaching solution. Non-ferrous metals such as lead and silver are stored in the leaching slag, and the leaching slag is returned to the fire method system to recover lead and silver and other metals. Precipitate copper and arsenic with caustic soda on the copper sulfate leaching solution, adjust pH to 4.5, leaching copper and arsenic slag with alkali, 20g / L sodium hydroxide...

Embodiment 2

[0052] Arsenic matte (Cu 45.22wt%, As 10.91wt%, Fe 5.24wt%, S 3.41wt%, Pb 15.66wt%, Sb 4.77wt%, Ag 2854g / t) was crushed, pulverized, and passed through a 100-mesh sieve. Take 150g arsenic matte powder with sulfuric acid solution and Cu 2+ Ions were added to the reaction kettle, the concentration of sulfuric acid solution was 100g / L, the temperature was set at 150°C, the liquid-solid ratio was 8:1 (mL / g), the oxygen partial pressure was 0.8MPa, Cu 2+ The amount of ions added is 5g / L, and the reaction time is 4h. After the leaching reaction is completed, liquid-solid separation is carried out to obtain a copper sulfate leaching solution. Non-ferrous metals such as lead and silver are stored in the leaching slag, and the leaching slag is returned to the fire method system to recover lead and silver and other metals. Precipitate copper and arsenic with caustic soda on the leaching liquid, adjust pH to 4.5, leaching copper and arsenic slag with alkali, 30g / L sodium hydroxide solut...

Embodiment 3

[0055] Arsenic matte (Cu 42.52wt%, As 13.76wt%, Fe 5.09wt%, S 4.14wt%, Pb 10.44wt%, Sb 5.87wt%, Ag 4154g / t) was crushed, pulverized, and passed through a 100-mesh sieve. Take 150g arsenic matte powder with sulfuric acid solution and Cu 2+ Ions are added to the reactor, the concentration of sulfuric acid solution is 80g / L, the temperature is set at 180°C, the liquid-solid ratio is 10:1 (mL / g), the oxygen partial pressure is 1.2MPa, Cu 2+ The amount of ions added is 8g / L, and the reaction time is 4h. After the leaching reaction is finished, liquid-solid separation is carried out to obtain a copper sulfate leaching solution. Non-ferrous metals such as lead and silver exist in the leaching slag, and the leaching slag is returned to the fire system to recover metals such as lead and silver. 4.5~5.0, alkaline leaching of copper arsenic slag, 40g / L sodium hydroxide solution, liquid-solid ratio 5:1 (mL / g), stirring in 80°C water bath for 2h, liquid-solid separation, solution containi...

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Abstract

The invention belongs to the field of chemical engineering, and discloses a method for efficiently separating copper arsenic in arsenic matte. The method includes the steps: (1) crushing the arsenic matte, grinding the crushed arsenic matte, and screening the grinded arsenic matte to obtain arsenic matte powder; (2) oxygen pressure leaching: performing oxygen pressure leaching on the arsenic mattepowder by the aid of sulfuric acid solution and Cu2<+> ions, and performing liquid solid separation after leaching is completed to obtain copper-containing leaching solution and lead-silver-containing leaching slag; (3) depositing the copper arsenic in the leaching solution, and performing alkaline leaching on copper arsenic slag to obtain alkaline leaching copper slag and high-arsenic-containing alkaline leaching solution; (4) fine lime arsenic depositing: adding fine lime into the alkaline leaching solution acquired in the step (3) to deposit the arsenic to obtain calcium arsenate. The method is simple in process and free from pollution, a works can not directly contact with harm of generated arsenide hydrogen in the production process, environments cannot be polluted, and precious metals such as copper, lead and silver in lead matte can be effectively recycled.

Description

technical field [0001] The invention belongs to the field of chemical industry and relates to wet treatment of arsenic matte, in particular to a method for efficiently separating copper and arsenic from arsenic matte. Background technique [0002] In the process of lead fire smelting, lead matte is often produced in the process of processing lead dross, and the output rate of matte is 0.5-2% of that of crude lead. Usually, we call lead matte with relatively high arsenic content It is called arsenic matte, and the arsenic content of arsenic matte is generally between 5% and 15%, and the copper content is also relatively high. Arsenic matte is an intermediate product with high value. It contains high content of copper, lead, gold, silver and other precious metals, but it also contains arsenic as an impurity element that is difficult to handle. How to remove arsenic from arsenic matte has become an industry difficulty. [0003] At present, there are many studies on the treatm...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/08C22B15/00C22B3/12C22B13/00C22B11/00C22B30/04
CPCC22B3/08C22B3/12C22B11/04C22B13/04C22B15/0071C22B30/04Y02P10/20
Inventor 段良洪刘伟高海明王敏杰曹文法
Owner CHENZHOU FENGYUE ENVIRONMENTAL PROTECTION TECH
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