Method for extracting nickel, cobalt and copper from nickel-copper alloy chloride leaching solution

A technology of chlorination leaching and nickel-copper alloy, which is applied in the fields of cobalt, copper, and nickel extraction, can solve the problems of long treatment process, low metal recovery rate, and high production cost, and achieve broad application range, low ionic strength, and reduced loose The effect of packing density

Inactive Publication Date: 2018-10-16
JINCHUAN GROUP LIMITED
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In order to solve the problems in the prior art that the leaching effect of the alloy is good, but the liquid treatment process after leaching is long, the metal recovery rate is low, the production cost of using ammonium oxalate as the precipitant is high, and the amount of wastewater is large and difficult to handle. Method for extracting nickel, cobalt and copper in nickel-copper alloy chloride leaching solution

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] A method for extracting nickel, cobalt, copper from nickel-copper alloy chlorination leach solution, described preparation method comprises the steps:

[0018] (1) Heat the chlorinated leaching solution to 70°C, slowly add liquid ammonia under stirring condition to adjust the pH value of the solution to 4, control the time of adding liquid ammonia for one hour, continue stirring for half an hour, and then filter the solution to obtain filtrate, filter residue Carry out curing treatment;

[0019] (2) The filtrate uses an extractant containing 15% 2-ethylhexyl phosphate mono-2-ethylhexyl ester and 85% sulfonated kerosene, and controls the saponification rate to 80%. Under the condition of O / A=5:1 Under the condition of extracting, cobalt and copper ions in the filtrate of extraction step (1), cobalt and copper enter the organic phase to form a loaded organic phase, and nickel remains in the raffinate in the form of nickel chloride;

[0020] (3) Use dilute hydrochloric ac...

Embodiment 2

[0027] A method for extracting nickel, cobalt, copper from nickel-copper alloy chlorination leach solution, described preparation method comprises the steps:

[0028] (1) Heat the chlorinated leaching solution to 60°C, slowly add liquid ammonia under stirring conditions to adjust the pH value of the solution to 4.5, control the time of adding liquid ammonia for one hour, continue stirring for half an hour, and then filter the solution to obtain the filtrate and filter residue Carry out curing treatment;

[0029] (2) The filtrate uses an extractant containing 25% 2-ethylhexyl phosphate mono-2-ethylhexyl ester and 75% sulfonated kerosene to control the saponification rate to 65%. Under the condition of O / A=5:1 Under the condition of extracting, cobalt and copper ions in the filtrate of extraction step (1), cobalt and copper enter the organic phase to form a loaded organic phase, and nickel remains in the raffinate in the form of nickel chloride;

[0030] (3) Use dilute hydrochl...

Embodiment 3

[0037] A method for extracting nickel, cobalt, copper from nickel-copper alloy chlorination leach solution, described preparation method comprises the steps:

[0038] (1) Heat the chlorinated leaching solution to 65°C, slowly add liquid ammonia under stirring condition to adjust the pH value of the solution to 45, control the time of adding liquid ammonia for one hour, continue stirring for half an hour, then filter the solution to obtain filtrate, filter residue Carry out curing treatment;

[0039](2) The filtrate uses an extractant containing 20% ​​2-ethylhexyl phosphate mono-2-ethylhexyl ester and 80% sulfonated kerosene, and controls the saponification rate to 70%. Under the condition of O / A=4:1 Under the condition of extracting, cobalt and copper ions in the filtrate of extraction step (1), cobalt and copper enter the organic phase to form a loaded organic phase, and nickel remains in the raffinate in the form of nickel chloride;

[0040] (3) Use dilute hydrochloric acid...

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Abstract

The invention relates to the field of wet metallurgy and chemical industry and particularly discloses a method for extracting nickel, cobalt and copper from a nickel-copper alloy chloride leaching solution. The method includes the steps that (1) the chloride leaching solution is heated, the pH value of the solution is adjusted by slowly adding liquid ammonia under the stirring condition, and the solution is filtered so as to obtain a filtrate; (2) the saponification rate is controlled through a 2-ethylhexyl phosphate mono-2-ethylhexyl ester and a sulfonated kerosene extraction agent, and cobalt and copper ions in the filtrate in the step (1) are extracted; (3) cobalt in a loaded organic phase in the step (2) is washed with diluted hydrochloric acid, and copper in the organic phase obtainedafter cobalt washing is finished is back-extracted through diluted sulphuric acid; (4) an ammonium hydrogen carbonate solution is reacted with an extraction raffinate in the step (2), the reaction endpoint is controlled, and nickel powder is obtained through reduction; (5) the ammonium hydrogen carbonate solution is reacted with a cobalt chloride washing solution in the step (3), the reaction endpoint is controlled, and cobalt powder is obtained through reduction; and (6) the copper sulfate back extraction solution in the step (3) is evaporated and crystallized, and then copper sulfate pentahydrate is obtained.

Description

technical field [0001] The invention relates to the fields of hydrometallurgy and chemical industry, in particular to a method for extracting nickel, cobalt and copper from nickel-copper alloy chlorinated leachate. Background technique [0002] The nickel-copper alloy produced during the pyro-smelting process of nickel sulfide ore contains valuable metals such as nickel, cobalt and copper, in addition to a small amount of elements such as iron, arsenic and lead. Nickel-cobalt-copper is the three most valuable metals among non-ferrous metals. The current main treatment process for this type of alloy is to leaching the alloy with hydrochloric acid and chlorine gas. The leaching solution is first extracted with copper-specific extractant, and then back-extracted with sulfuric acid to obtain a high-acid copper sulfate solution for the production of electrolytic copper. The raffinate after extracting copper is removed with P204, cobalt is extracted with C272, and back-extracted ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B15/00C22B23/00C22B3/38C22B3/44C22B3/14
CPCC22B3/14C22B3/44C22B15/0084C22B23/0453C22B23/0461C22B3/3844Y02P10/20
Inventor 陈国栋何子川龚继宝王文鹏冯泽树
Owner JINCHUAN GROUP LIMITED
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