A Recycling Process of Refractory and Complex Polymetallic Ore
A polymetallic ore and refractory technology, applied in the direction of non-metallic elements, process efficiency improvement, inorganic chemistry, etc., can solve the problems of low recovery rate of valuable elements, environmental pollution, high equipment requirements, etc., to achieve clean and pollution-free process, The effect of less process hazard and less investment
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Embodiment 1
[0030] A recycling process for difficult and complex polymetallic ore, such as figure 1 As shown, including the following steps:
[0031] Step (1), oxygen pressure leaching of polymetallic ore: After ball milling the polymetallic ore, pass through a 320-mesh sieve, add the acid solution to the pressure vessel, add the material according to the mass ratio of the acid solution to the polymetallic ore at 4.5:1, then seal and pass Enter oxygen and heat and stir for leaching. Control the leaching conditions: 150~160℃, oxygen partial pressure 0.8MPa, leaching time 4h, solution pH value 1-3; after leaching is completed, filter and analyze the filter residue. Wherein, the acid solution is zinc extraction residue, in which the concentration of sulfuric acid is 80g / L;
[0032] The comprehensive leaching rates of valuable metals are respectively: Cu96.7%, Zn95.3%, Fe13.4%, and gold, silver, lead, arsenic, and sulfur are basically retained in the leaching residue. The main element content (%)...
Embodiment 2
[0046] A recycling process for difficult and complex polymetallic ore, such as figure 1 As shown, including the following steps:
[0047] Step (1), oxygen pressure leaching of polymetallic ore: After ball milling the polymetallic ore, pass through a 320-mesh sieve, add the acid solution to the pressure vessel, add the material according to the mass ratio of the acid solution to the polymetallic ore 4:1, then seal and pass Enter oxygen and heat and stir for leaching. Control the leaching conditions: 170~180℃, oxygen partial pressure 0.5MPa, leaching time 6h, solution pH value 1-3; after leaching is completed, filter and analyze the filter residue. Wherein, the acid solution is zinc extraction residue, in which the concentration of sulfuric acid is 75g / L;
[0048] The comprehensive leaching rates of valuable metals are respectively: Cu96.2%, Zn95.1%, Fe13.0%, and gold, silver, lead, arsenic, and sulfur are basically retained in the leaching residue. The main element content (%) of t...
Embodiment 3
[0062] A recycling process for difficult and complex polymetallic ore, such as figure 1 As shown, including the following steps:
[0063] Step (1), oxygen pressure leaching of polymetallic ore: After ball milling the polymetallic ore, pass through a 320-mesh sieve, add the acid solution to the pressure vessel, add the material according to the mass ratio of the acid solution to the polymetallic ore at 5:1, then seal and pass Enter oxygen and heat and stir for leaching. Control the leaching conditions: 160~170℃, oxygen partial pressure 0.2MPa, leaching time 1h, solution pH value 1-3; after leaching is completed, filter and analyze the filter residue. Wherein, the acid solution is an aqueous sulfuric acid solution, wherein the concentration of sulfuric acid is 80 g / L;
[0064] The comprehensive leaching rates of valuable metals are respectively: Cu97.5%, Zn95.8%, Fe14.1%, and gold, silver, lead, arsenic, and sulfur are basically retained in the leaching residue. The main element con...
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