Method for efficiently enriching rare precious metals from complex low-grade heat filter residues

A low-grade heat, rare and precious metal technology, applied in the improvement of process efficiency, thiosulfate/dithionite/polythionite, etc., can solve the dispersion loss of rare and precious metals, large material turnover, valuable Metal flying and other problems, to achieve the effect of good comprehensive utilization, high enrichment ratio and large processing capacity

Active Publication Date: 2014-12-24
JINCHUAN GROUP LIMITED
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This treatment method has a long process flow and a large turnover of materials. Some precious metals and sulfur elements are circulated in it and dispersed in the nickel and cobalt refining system. The other part of the hot filter residue is stored in the open air for a long time due to no suitable treatment method. It caused the flying and loss of valuable metals, and some of them were incinerated. The incineration slag was granulated and incorporated into the alloy converter for treatment, which polluted the environment and caused the dispersion loss of rare and precious metals.

Method used

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  • Method for efficiently enriching rare precious metals from complex low-grade heat filter residues
  • Method for efficiently enriching rare precious metals from complex low-grade heat filter residues
  • Method for efficiently enriching rare precious metals from complex low-grade heat filter residues

Examples

Experimental program
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Effect test

Embodiment 1

[0048] Crushing and classifying the hot filter residue to obtain the raw material with a particle size not greater than 120 mesh; the chemical composition of the hot filter residue is shown in Table 1.

[0049] Table 1 Chemical composition of hot filter residue

[0050]

[0051]According to the ratio of adding 1kg of raw materials to 6 liters of dilute sulfuric acid, add the raw materials into the dilute sulfuric acid solution with a mass volume concentration of 5g / L, and perform a period of normal pressure leaching at a temperature of 80°C. After leaching for 1 hour, measure the pH value of the leachate , if the pH value of the leaching solution is 1.0 to 3.0, the leaching is finished, filtered and washed to obtain a section of normal pressure leaching solution and a section of normal pressure leaching residue; the chemical composition of a section of normal pressure leaching residue is shown in Table 2.

[0052] Table 2 Chemical composition of the leaching slag from the...

Embodiment 2

[0083] Crushing and classifying the hot filter residue to obtain the raw material with a particle size of not more than 120 mesh; the chemical composition of the hot filter residue is shown in Table 10.

[0084] Table 10 Chemical composition of hot filter residue

[0085]

[0086] According to the ratio of adding 1kg of raw materials to 10 liters of dilute sulfuric acid, add the raw materials into the dilute sulfuric acid solution with a mass volume concentration of 15g / L, and perform a period of normal pressure leaching at a temperature of 90°C. After 4 hours of leaching, measure the pH value of the leachate , if the pH value of the leaching solution is 1.0 to 3.0, the leaching is completed, filtered and washed to obtain a section of normal pressure leaching solution and a section of normal pressure leaching residue; the chemical composition of a section of normal pressure leaching residue is shown in Table 11.

[0087] Table 11 Chemical composition of leaching slag from t...

Embodiment 3

[0118] Crushing and grading the hot filter residue to obtain the raw material with a particle size of no more than 120 mesh; add the raw material to the dilute sulfuric acid solution with a mass volume concentration of 8g / L according to the ratio of adding 1kg of raw material to 8 liters of dilute sulfuric acid, and heat it at a temperature of 85°C Carry out a section of normal pressure leaching, after 2.5 hours of leaching, measure the pH value of the leachate, if the pH value of the leachate is 1.0 to 3.0, then the leaching is over, filter and wash, and obtain a section of normal pressure leachate and a section of normal pressure leaching residue; initially, the Add water into the reactor, add 300g of anhydrous sodium sulfite per liter of water, add anhydrous sodium sulfite into the mixed solution, after dissolving, add a period of normal pressure leaching residue according to the liquid-solid ratio of 6:1, and then add a concentration of 10 % sodium hydroxide solution, so th...

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Abstract

The invention provides a method for efficiently enriching rare precious metals from complex low-grade heat filter residues. The method comprises the following steps: performing first-stage normal-pressure preliminary leaching and second-stage normal-pressure desulfurization leaching on the heat filter residues; performing evaporation, concentration and crystallization on a first-stage desulfurization liquid to obtain a sodium thiosulfate product; performing pressurization oxidation leaching on second-stage desulfurization residues; and removing silicon, iron, barium, calcium magnesium, aluminum, complex silicates and the like from glass residues prepared from pressurized residues, thereby obtaining a high-grade product rich in precious metals. The method is simple in process, environmentally-friendly, free of generation of toxic waste gases, gas residues and like as well as free of usage of toxic reagents, thereby being favorable for environmental protection. The method is easy to operate, low in working intensity, high in efficiency and easy in production process control and capable of easily realizing the process automation. According to the method, a high-grade and good-quality precious metal concentrate in which the content of gold, silver and platinum group metals can be 9% to 15% is obtained; and the recovery rate of the precious metals can be more than 99%. Thus, the method provided by the invention can be easily matched with an extraction separation refining process of the gold and platinum group metals.

Description

technical field [0001] The invention belongs to the technical field of rare and precious metal hydrometallurgy, and relates to a method for separating and extracting rare and precious metals from sulfur molten hot filter residues, in particular to a method for efficiently enriching rare and precious metals from complex and low-grade hot filter residues. Background technique [0002] In the metallurgical process of extracting nickel and cobalt containing rare precious metals, especially copper-nickel sulfide ores, the copper-nickel high matte containing gold and platinum group metals is processed by crushing, grinding, grading, magnetic separation, flotation and other processes to obtain gold and platinum Primary alloys of group metals, copper concentrates and nickel concentrates with low copper content (Cu2~5%, Ni63~67%, S22~24%). The nickel concentrate is melted in a reverberatory furnace and cast into an anode plate (called a high matte anode plate), and then subjected to ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/00C22B11/00C01B17/64
CPCY02P10/20
Inventor 宋宏儒吴建明郭少敏张燕王玉刚陈云峰
Owner JINCHUAN GROUP LIMITED
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