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
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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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