Unlock instant, AI-driven research and patent intelligence for your innovation.

Deep impurity removal technology for coarse gold powder

A technology for deep impurity removal and rough gold, applied in the direction of improving process efficiency, can solve the problems of increased content, unreachable, difficult to control silver, etc., and achieve the effect of reducing the content of impurity elements

Active Publication Date: 2013-01-09
JINCHUAN GROUP LIMITED
View PDF0 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At home and abroad, the fire process is often used to treat copper anode slime. Our company also successfully applied this process to production in 2000. The main process is to produce gold by electrolysis of coarse gold powder produced in the gold separation process. The principle process is copper anode slime sulfuric acid chemical roasting—acid leaching to separate copper—alkali leaching to separate tellurium—chlorination to separate gold—reduction of coarse gold powder—liquidation electrolysis—electrolysis of gold plate—boiling and washing to remove impurities. The requirements are high, especially the impurity element silver in the electrolytic gold plate is difficult to control
Due to the sharp increase of impurity elements in copper raw materials in recent years, the quality of coarse gold powder produced in the roasting and leaching process of copper anode slime has declined significantly, mainly because the content of impurity elements such as silver, lead, antimony, and bismuth has increased, which eventually leads to electrolytic production. The quality of the gold products produced is difficult to meet the standard
For this reason, a new wet process was adopted to replace the electrolytic method to refine the crude gold powder. The quality of the gold powder produced still cannot meet the requirements of the national standard IC-Au99.99. Therefore, it is urgent to find a new process for the deep removal of impurities in coarse gold powder.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Put the crude gold powder into the chlorination leaching kettle, control the liquid-solid ratio of 14:1, add industrial hydrochloric acid to control the acidity of the solution to 3mol / L, the volume is 800L, and the temperature is 80°C, then carry out chlorine leaching for 12 hours, then cool and discharge the material and filter . Transfer the filtrate to the hydrolysis kettle, heat up and boil, concentrate the volume to 200L, cool, add deionized water to the volume of the original solution to 800L, stir for 30min, let it stand for 2h, discharge the material and filter, transfer the hydrolyzed liquid to the hydrolysis kettle to concentrate—add Deionized water-stirring-static filtration repeats the hydrolysis treatment for 3 times and then carries out gold reduction. The hydrolysis slag is stored in a centralized manner, and the content of silver, lead, antimony and bismuth is reduced by 94.2%.

Embodiment 2

[0020] Put the crude gold powder into the chlorination leaching kettle, control the liquid-solid ratio of 15:1, add industrial hydrochloric acid to control the acidity of the solution to 3mol / L, the volume is 800L, and the temperature is 85°C, then carry out chlorine leaching for 10 hours, then cool and discharge and filter . Transfer the filtrate to the hydrolysis kettle, heat up and boil, concentrate the volume to 300L, cool, add deionized water to the volume of the original solution to 800L, stir for 60min, let it stand for 2h, discharge and filter, and transfer the hydrolyzed liquid to the hydrolysis kettle to concentrate—add Deionized water-stirring-static filtration repeats the hydrolysis treatment for 2 times, followed by gold reduction, and the hydrolysis slag is stored in a centralized manner, and the content of silver, lead, antimony and bismuth is reduced by 95.1%.

Embodiment 3

[0022] Put the crude gold powder into the chlorination leaching tank, control the liquid-solid ratio of 16:1, add industrial hydrochloric acid to control the acidity of the solution to 3mol / L, the volume is 800L, and the temperature is 83°C, then carry out chlorine leaching for 14 hours, then cool down and filter . Transfer the filtrate to the hydrolysis kettle, heat up and boil, concentrate the volume to 260L, cool, add deionized water to the volume of the original solution to 800L, stir for 50min, let it stand for 2h, discharge and filter, and transfer the hydrolyzed liquid to the hydrolysis kettle to concentrate—add Deionized water-stirring-static filtration repeats the hydrolysis treatment for 3 times and then carries out gold reduction. The hydrolysis slag is stored in a centralized manner, and the content of silver, lead, antimony and bismuth is reduced by 94.7%.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention provides a deep impurity removal technology for coarse gold powder, which comprises the following steps: putting the coarse gold powder into a chloridizing leaching reactor according to the liquid-solid ratio of (14-16):1, controlling the acidity of solution to be 3mol / L by adding industrial hydrochloric acid, and leaching by introducing chlorine after the temperature reaches 80-85 DEG C for 10-14 hours; then cooling, discharging and filtering, heating and boiling a filtrate and concentrating the volume to be 25% to 37.5% of the original volume, adding deionized water to the original volume after cooling, stirring for 30-60 minutes, standing for 2 hours and then discharging and filtering; and after hydrolysis, repeatedly operating steps of concentrating, deionized water adding, stirring, standing and filtering to remove impurities by hydrolysis, carrying out gold reduction after 2 to 3 times of hydrolysis treatment, and intensively storing hydrolysis residues. Through the process, the impurity content in the solution not subject to the gold reduction is effectively reduced, and especially the contents of Ag, Sb, Pb and Bi are decreased by 95% or so.

Description

technical field [0001] The invention relates to a hydrometallurgical process in the field of metallurgy, in particular to a coarse gold powder deep impurity removal technology for effectively removing most of the impurity elements such as silver and antimony in the coarse gold powder chlorination solution. Background technique [0002] At home and abroad, the fire process is often used to treat copper anode slime. Our company also successfully applied this process to production in 2000. The main process is to produce gold by electrolysis of coarse gold powder produced in the gold separation process. The principle process is copper anode slime sulfuric acid chemical roasting—acid leaching to separate copper—alkali leaching to separate tellurium—chlorination to separate gold—reduction of coarse gold powder—liquidation electrolysiselectrolysis of gold plate—boiling and washing to remove impurities. The requirements are high, especially the impurity element silver in the electr...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/46C22B11/00
CPCY02P10/20
Inventor 陈大林赵彦才潘从明李明张燕许银风
Owner JINCHUAN GROUP LIMITED