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Application of anthraquinone-2-sodium sulfonate in cyaniding and leaching high-grade gold in oxidized ore

A sodium sulfonate, high-grade technology, applied in the direction of organic compound/hydride/coordination complex catalyst, physical/chemical process catalyst, process efficiency improvement, etc., can solve the problem of high cost of equipped control system and slow gold leaching speed , high cyanide consumption and other problems, to achieve the effect of increasing the gold leaching rate and leaching speed, increasing the gold leaching rate, and reducing the cyanide consumption

Inactive Publication Date: 2011-04-13
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The cyanide leaching reaction of gold is to dissolve the gold in the mineral material in the alkaline cyanide medium with the participation of oxygen. At present, the method of adding oxygen to the slurry is generally used. This method is suitable for processing low-grade mineral materials. However, when dealing with high-grade mineral materials, due to the limited amount of dissolved oxygen in the slurry, and the speed at which oxygen transfers from the gas phase into the mortar and diffuses to the surface of the gold particles is too slow, it cannot meet the requirements of high-grade minerals. The requirement of gold for oxygen supply causes the leaching speed of gold to be slow, the leaching rate is low and the consumption of cyanide is large; "Sand Metallurgy Engineering" 1993Vol. The experimental research situation of "Application in China", the test shows that the liquid oxidant hydrogen peroxide (H 2 o 2 ) can shorten the leaching time, increase the leaching rate of gold and reduce the consumption of cyanide, but its oxidizing property is too strong. When the dosage is large, it can not only oxidize gold, but also oxidize the leaching agent cyanide, and even make some gold The particles are passivated due to excessive oxidation. With the increase of the amount of hydrogen peroxide, the leaching of gold first increases and then decreases. Therefore, when using H 2 o 2 When assisting gold leaching, a corresponding control system must be equipped to control the H in the slurry. 2 o 2 concentration (this is the H 2 o 2 The key to the immersion method), but the cost of the control system is relatively high, so its application is limited

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] A high-arsenic-encapsulated gold-bearing sulfide ore in Hunan, the ore is a high-arsenic fine-grained gold ore, and the gold is wrapped in arsenic pyrite and pyrite in a fine-grained state (the gold embedded particle size is generally 0.005-0.043mm) , The gangue minerals are mainly quartz. The flotation gold concentrate is roasted in two stages to produce loose and porous calcined sand (containing gold 110g / t), which is treated according to the method of the present invention after ore washing. The technological conditions adopted are: the grinding fineness is less than 43 μm, accounting for more than 95%, the liquid-solid ratio is 2:1, the slurry pH is 10-11 (adjusted with lime), other test conditions and test results are shown in Table 1, for convenience The data for compressed air are listed in Table 1 for comparison.

[0030] Test conditions and results under different oxygen supply conditions (Table 1)

[0031]

Embodiment 2

[0033] A packaged gold sulfide deposit in Guizhou, the main metal minerals are pyrite, arsenopyrite and realgar, a small amount of chalcopyrite, galena and sphalerite, and the gangue minerals are mainly quartz. Gold minerals are mainly natural gold, which is closely related to sulfide. The distribution rate of gold wrapped in pyrite and arsenopyrite accounts for more than 99%, and the embedded gold particle size is generally 0.006-0.039mm. The flotation gold concentrate is roasted in two stages to produce high-grade gold oxidized calcined sand (containing 82g / t gold), and after washing (dilute acid medium), the product is processed according to the method of the present invention. Grinding fineness less than 39μm accounts for more than 80%, the liquid-solid ratio is 2:1, the slurry pH is 10-11 (adjusted with sodium hydroxide), and other test conditions and test results are shown in Table 2. For comparison, Table 2 also lists The data for compressed air is shown.

[0034] Test...

Embodiment 3

[0038]A fine-grained wrapped sulfide gold sand in Yunnan, the main metal minerals are pyrite, arsenopyrite and orthorhombic arsenite, a small amount of galena and sphalerite, and the main gangue minerals are quartz, feldspar, green Mudstone and calcite. Gold is mainly natural gold, which is closely related to sulfide. The distribution rate of gold wrapped in pyrite, arsenopyrite and orthorhombic arsenopyrite accounts for more than 90%. The gold embedded particle size is very fine, less than 37μm Accounted for 97%, less than 10μm accounted for 30%. The flotation gold concentrate is roasted in two stages to produce loose and porous calcined sand (containing 55g / t of gold), and after washing and grinding, the product is processed according to the method of the present invention. Grinding fineness less than 37μm accounts for more than 97%, the liquid-solid ratio is 2:1, and the pH of the slurry is 10-11 (adjusted with sodium hydroxide). Other test conditions and results are shown...

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PUM

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Abstract

The invention relates to application of anthraquinone-2-sodium sulfonate in cyaniding and leaching high-grade gold in oxidized ore, in particular to application of anthraquinone-2-sodium sulfonate as a catalyst for oxidizing and slowly releasing H2O2 in the cyaniding and leaching reaction of gold. The invention can be realized on the traditional equipment and has the advantages of low cost of used anthraquinone-2-sodium sulfonate, convenient preparation and wide raw material source, and a product of leaching reaction does not influence the following treatment operation. As far as ore property is concerned, the anthraquinone-2-sodium sulfonate is used for catalyzing and leaching gold and has higher competitiveness on treating high-grade gold oxidized ore obtained after carrying out preoxidation treatment (oxidation roasting, pressure heating oxidation and bacterial oxidation) on floating gold concentrate ore of coated type vulcanized gold ore.

Description

technical field [0001] The invention relates to a method for leaching gold by cyanide, which is to apply sodium anthraquinone-2-sulfonate in the method as an oxidation and slow-release H 2 o 2 catalyst. Background technique [0002] With the continuous mining of gold resources, the easy-to-handle gold mines are increasingly exhausted, so the utilization and development of refractory gold mines will become a key issue in the development of my country's gold industry. [0003] Encapsulated sulfide gold ore (gold wrapped in sulfide mineral lattice) is the most typical refractory gold ore. The typical treatment process is to pre-process the sulfide ore gold concentrate obtained from the flotation (enrichment of gold) of the raw ore. Oxidation (oxidative roasting, autoclave oxidation and bacterial oxidation) to destroy the sulfide mineral lattice to expose the gold particles, and then oxygenate the high-grade gold (50-120g / t) in the oxidized ore (compressed air or pure oxygen)...

Claims

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Application Information

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IPC IPC(8): B01J31/02C22B11/08C22B3/12
CPCY02P10/20
Inventor 张鹏飞赵甜香叶红齐
Owner CENT SOUTH UNIV
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