Method for preparing high-purity rhenium powder from rhenium-containing high-arsenic copper sulfide
A copper sulfide, high-purity technology, applied in the field of preparation of high-purity rhenium powder, to achieve high yield, simple process, and good industrial application prospects
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Embodiment 1
[0032] See attached figure 1 , Conditions: 1000 grams of rhenium-arsenic copper sulfide raw material, the amount of nitric acid added is twice the weight ratio of rhenium-arsenic copper sulfide raw material, slowly heated to 85°C, stirring speed is 250rpm, leaching time is 5h, the flue gas enters the absorption tower , using oxygen enrichment and water spray absorption to form dilute nitric acid. After leaching, filter and wash to obtain leaching solution and leaching residue respectively. Add quicklime to the leaching solution and stir to neutralize residual nitric acid, control the pH to 8.5, filter and wash to obtain Arsenic-copper slag and low-content rhenium-containing filtrate, wherein the arsenic and copper in the slag enter the slag in the form of calcium arsenate and copper hydroxide respectively; the low-content rhenium-containing filtrate uses D296 resin for ion exchange, and after exchange and elution, pure Ammonium rhenate solution is heated and concentrated, and ...
Embodiment 2
[0034] See attached figure 1 , conditions: 1500 grams of rhenium-arsenic-containing copper sulfide raw materials, the amount of nitric acid added is 3.5 times the weight ratio of rhenium-arsenic-containing copper sulfide raw materials, slowly heated to 95°C, stirring speed is 250rpm, leaching time is 4h, and the flue gas enters the absorption tower , using sodium persulfate and water spray absorption to form dilute nitric acid, after leaching, filter and wash to obtain leaching solution and leaching residue respectively, add hydrated lime to the leaching solution and stir to neutralize residual nitric acid, control pH to 9.0, filter and wash, respectively Obtain arsenic-copper slag and low-content rhenium-containing filtrate, wherein the arsenic and copper in the slag enter the slag in the form of calcium arsenate and copper hydroxide respectively; the low-content rhenium-containing filtrate uses Tulsion CR-75 resin for ion exchange, after exchange and washing After desorption...
Embodiment 3
[0036] See attached figure 1 , conditions: 8000 grams of rhenium-arsenic-containing copper sulfide raw materials, the amount of nitric acid added is 4.0 times the weight ratio of rhenium-arsenic copper sulfide-containing raw materials, slowly heated to 85°C, stirring speed is 250rpm, leaching time is 5h, and the flue gas enters the absorption tower , use hydrogen peroxide and water spray to absorb, form dilute nitric acid, after leaching, filter and wash to obtain leaching solution and leaching residue respectively, add hydrated lime to the leaching solution and stir to neutralize residual nitric acid, control pH to 9.5, filter and wash to obtain arsenic Copper slag and low-content rhenium-containing filtrate, wherein the arsenic and copper in the slag enter the slag in the form of calcium arsenate and copper hydroxide respectively; the low-content rhenium-containing filtrate uses Tulsion RCX-5143 resin for ion exchange, after exchange and elution, Obtain pure ammonium rhenate...
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