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Technological method for extracting antimony and bismuth from rare and noble metallurgical slag

A technology of rare and precious metals and process methods, which is applied in the field of extracting antimony and bismuth from rare and precious metal smelting slag, which can solve the problems of increased energy consumption, unrecoverable antimony and bismuth elements, and waste of valuable resources, and achieve the effect of improving efficiency

Inactive Publication Date: 2015-09-09
铜陵有色金属集团股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The technical problem to be solved by the present invention is that the existing recycling of rare and precious metal smelting slag only recovers gold and silver elements, resulting in products containing a large amount of antimony and bismuth elements that cannot be recycled, product quality declines, energy consumption increases, and valuable resources such as antimony and bismuth are wasted , to provide a process for extracting antimony and bismuth from rare and precious metal smelting slag gold concentrate

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0008] Example 1: (1), leaching, adding rare precious metal smelting slag to the leaching reactor, then adding industrial sulfuric acid at a mass ratio of smelting slag: sulfuric acid of 2:1, and adding chlorine at a mass ratio of smelting slag: sodium chloride of 0.6:1 Sodium chloride, control the solid-liquid ratio in the reactor to 1: 5, control the temperature of the leachate at 90°C, stir for 3 hours under normal pressure, let stand and cool to clarification, and press filter to obtain the leach residue and press filter solution after impurity removal and separation; ( 2) For the separation of antimony, control the temperature of the filter press solution at 30°C, add water 5 times the volume of the filter press solution and adjust the pH value of the filter press solution to 0.5 by adding sodium hydroxide, stir under normal pressure and let stand for 1.5h, filter , to obtain antimony oxychloride and antimony-precipitated solution; (3) for the separation of bismuth, add so...

Embodiment 2

[0009] Example 2: (1), leaching, adding rare precious metal smelting slag gold concentrate to the leaching reactor, then adding industrial sulfuric acid according to the gold concentrate: sulfuric acid mass ratio of 3:1, according to the gold concentrate: sodium chloride mass ratio is Add sodium chloride at 0.8:1, control the solid-to-liquid ratio in the reactor to 1:5.5, control the temperature of the leachate at 93°C, stir for 3 hours under normal pressure, leave to cool until clarified, and press filter to obtain the leach residue after impurity removal and separation. Press filter solution; (2) For the separation of antimony, control the temperature of the press filter solution at 35°C, add water 5 times the volume of the press filter solution and adjust the pH value of the press filter solution to 0.7 by adding sodium hydroxide, stir under normal pressure and then statically Set aside for 1.5h and filter to obtain antimony oxychloride and antimony-precipitated liquid; (3) ...

Embodiment 3

[0010] Embodiment 3: (1), leaching, add rare precious metal smelting slag gold concentrate to leaching reactor, then add industrial sulfuric acid according to gold concentrate: sulfuric acid mass ratio 4:1, according to gold concentrate: sodium chloride mass ratio is Add sodium chloride at 1:1, control the solid-liquid ratio in the reactor to 1:6, control the temperature of the leaching solution at 95°C, stir for 3 hours under normal pressure, let it stand and cool until clarification, and then press filter to obtain the leaching residue after impurity removal and separation. Press filter solution; (2) For the separation of antimony, control the temperature of the press filter solution at 40°C, add water 5 times the volume of the press filter solution and adjust the pH value of the press filter solution to 1 by adding sodium hydroxide, stir under normal pressure and then statically Set aside for 1.5h, filter to obtain antimony oxychloride and antimony-precipitated solution; (3)...

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PUM

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Abstract

The invention discloses a technological method for extracting antimony and bismuth from rare and noble metallurgical slag. The technological method comprises the following steps: (1) performing leaching: adding rare and noble metallurgical slag gold concentrates to a leaching reaction kettle, then adding an industrial sulfuric acid with the mass ratio of the gold concentrates to the sulphuric acid being 2-4:1, adding sodium chloride with the mass ratio of the gold concentrates to the sodium chloride being 0.6-1:1, leaving a solution in the leaching reaction kettle to stand, cooling the solution after standing until clarification, and then performing pressure filtration so as to obtain the leached slag and pressure filtration solutions, on which slag removal and separation are performed; (2) separating antimony so as to obtain antimonous oxychloride and an antimony precipitation solution; (3) separating bismuth so as to obtain bismuth oxide chloride. The technological method disclosed by the invention has the benefits that under the premise that the recovery of noble metals, such as gold and silver, is ensured not to be influenced, firstly, valuable elements of antimony and bismuth are separated from the gold concentrates, on one hand, antimony resources and bismuth resources are recovered, and the benefit is promoted; on the other hand, a favorable raw material condition is created for the subsequent recovery of gold, silver and the like through smelting.

Description

technical field [0001] The invention relates to a rare and precious metal purification treatment process, in particular to a process for extracting antimony and bismuth from rare and precious metal smelting slag. Background technique [0002] After various rare and precious metal raw materials are smelted at a high temperature of about 1000~1200°C, precious metals and corresponding smelting slags are produced. The smelting slag contains a small amount of gold, silver and a large amount of valuable elements such as antimony and bismuth mixed in multivalent states. Usually, this part of the smelting slag is directly returned to the copper and lead smelting system or the gold concentrate after flotation is returned to the gold and silver collection system, only the main elements of gold and silver are recovered, and the antimony and bismuth elements cannot be recovered. The main elements of gold and silver are recovered by direct smelting. Due to the high content of antimony an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/04C22B30/02C22B30/06
CPCY02P10/20
Inventor 梁海卫朱新生龚昌合李春侠
Owner 铜陵有色金属集团股份有限公司
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