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Harmless treatment method of arsenic-bearing slag liquid of biological preoxidation-cyanidation gold extracting process of arsenic-bearing gold concentrate

A technology of harmless treatment and pre-oxidation, applied in the direction of improving process efficiency, can solve problems such as poor stability of arsenic-containing cyanide tailings, and achieve the effects of high stability, low slag rate and high stability

Active Publication Date: 2016-05-11
厦门紫金矿冶技术有限公司
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the slow biological preoxidation process, the gold leaching rate in the cyanide carbon leaching process is mainly used as the main technical index in the biological preoxidation-cyanidation gold extraction process, and to achieve an economically reasonable gold comprehensive recovery rate, gold-loaded sulfide The oxidation rate of the sulfide is generally lower than 100%, and the lowest can reach 50%, that is, there are still most of the gold-loaded sulfides that have not been completely oxidized, resulting in a certain amount of reduced substances in the biological pre-oxidation slag.
At the same time, if the solid-liquid separation of the pre-oxidized pulp is not complete, part of the free As and iron will be carried into the cyanidation system by the pre-oxidized slag, and arsenic-containing precipitates similar to those precipitated by the "lime-iron-salt method" will be formed during the cyanidation alkali adjustment process. The stability of arsenic-containing cyanidation tailings is still poor

Method used

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  • Harmless treatment method of arsenic-bearing slag liquid of biological preoxidation-cyanidation gold extracting process of arsenic-bearing gold concentrate
  • Harmless treatment method of arsenic-bearing slag liquid of biological preoxidation-cyanidation gold extracting process of arsenic-bearing gold concentrate
  • Harmless treatment method of arsenic-bearing slag liquid of biological preoxidation-cyanidation gold extracting process of arsenic-bearing gold concentrate

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Experimental program
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Effect test

Embodiment 1

[0032] Embodiment 1 (comparative example)

[0033] Conventional treatment process: Weigh 2kg of gold concentrate, use 9K medium as nutrients, gold concentrate -45μm particle size accounts for 75%, pulp concentration 18%, temperature 40-42°C, initial pH value of oxidation is 1.6, stirring speed is 550rpm, oxidation time of 6 days, dissolved oxygen amount of 1-2ppm, pH value of the solution after oxidation is 0.6, iron ion concentration of 17g / L, arsenic concentration of 2g / L, and finally the oxidation rate of sulfide is 90%. After oxidation, the liquid is adjusted to pH 4.0 with limestone, and then adjusted to pH 9.0 with lime. The concentration of iron ions is 0.44mg / L, and the concentration of arsenic is 0.01mg / L. The separation performance is poor, and the analysis results of the form distribution of arsenic in the slag are shown in Table 1; the carbon leaching conditions of the oxide slag are: time 24 hours, pH 10, activated carbon dosage 20g / L, sodium cyanide dosage 4kg / t ...

Embodiment 2

[0035] Such as figure 1 shown, including the following steps:

[0036](1) 2 kg of arsenic-containing gold concentrate is pre-oxidized with a bio-tank leaching process to obtain pre-oxidized ore pulp. The specific parameters of the bio-tank leaching are as follows: 9K medium is used as a nutrient substance, the ore-45 μm particle size accounts for 75%, and the temperature is 40-42°C, the time is 6 days, the pulp concentration is 18%, the initial pH is 1.6, the stirring speed is 550rpm, the dissolved oxygen is 1-2ppm, the pH of the obtained pre-oxidized pulp is 0.6, the iron ion concentration is 17g / L, The arsenic concentration is 2g / L, and the oxidation rate of sulfide is 90%;

[0037] (2) Carrying out solid-liquid separation to the above-mentioned preoxidized ore pulp to obtain the first supernatant and the first underflow;

[0038] (3) Pre-neutralize the first supernatant with gold concentrate to pH = 2.0-2.5 and then separate the solid and liquid to obtain the second super...

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Abstract

The invention discloses a harmless treatment method of arsenic-bearing slag liquid of the biological preoxidation-cyanidation gold extracting process of arsenic-bearing gold concentrate. The method includes the steps of firstly, pre-oxidizing the arsenic-bearing gold concentrate with a biological tank leaching process to obtain pre-oxidized ore pulp; secondly, performing solid-liquid separation on the pre-oxidized ore pulp to obtain first supernate and first underflow; thirdly, pre-neutralizing the first supernate, and performing solid-liquid separation on the pre-neutralized first supernate to obtain second supernate and second underflow; fourthly, performing goethite iron precipitation and arsenic fixing on the second supernate for 2-4 hours, and then performing solid-liquid separation to obtain overflow liquid and third underflow, allowing the overflow liquid to enter the biological tank leaching process, allowing part of the third underflow serving as seed crystal to return to the reaction device of the iron precipitation and arsenic fixing, and discharging the rest of third underflow; fifthly, performing cyanidation carbon-in-pulp leaching on the first underflow to obtain ore pulp; sixthly, performing ferric salt aeration arsenic fixing on the ore pulp obtained in the fifth step. The method provides necessary technical support for the environment-friendly, efficient and low-cost development of the arsenic-bearing gold concentrate.

Description

technical field [0001] The invention belongs to the technical field of mineral waste slag treatment, and in particular relates to a method for harmlessly treating arsenic-containing slag liquid of arsenic-containing gold concentrate biological pre-oxidation-cyanidation gold extraction process. Background technique [0002] The two famous Golden Triangles of "Yunnan, Guizhou, Guangxi" and "Shaanxi, Gansu and Sichuan" in my country contain a large amount of low-grade refractory gold concentrates, the gold grade is only 1-6g / t, and it is mainly composed of pyrite and arsenopyrite. The sulfide is wrapped in the gold-loaded sulfide and even exists in the form of lattice gold in the gold-loaded sulfide. At the same time, the particle size of the gold-loaded mineral itself is fine, especially accompanied by a large amount of arsenic and organic carbon. concentrate. This kind of ore is directly cyanided, the gold leaching rate is low, and the amount of sodium cyanide is huge, so it i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/18C22B11/08
CPCY02P10/20
Inventor 黄怀国庄荣传林鸿汉季常青范道焱叶志勇李黎婷董博文
Owner 厦门紫金矿冶技术有限公司
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