Extraction method of valuable elements from acid mud produced in sulfuric acid production by copper smelting flue gas
A technology of valuable elements and extraction methods, applied in the direction of element selenium/tellurium, improvement of process efficiency, etc., can solve the problem of low recovery rate of selenium, and achieve good and efficient separation effects
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Embodiment 1
[0050] Dry the acid mud and crush it to 120 mesh. The main components in the acid mud are calculated as (%) by mass percentage: Pb37.40, Se40.74, As3.14, Hg2.25. Take by weighing lime powder 28.4g, 50% lime powder is added in the selenium acid mud of 50g above-mentioned composition, mix homogeneously, place in the muffle furnace after remaining lime content is covered on the mixture surface, control roasting temperature is 450°C, roasting time 8h, after reaching the reaction time, weigh after cooling, the mercury-removed slag weighs 82.2g, and its main components are (%) by weight: Se24.8, As1.85, Hg0.14. The volatilization rates of Se, Hg, and As are 0, 99%, and 2.95%, respectively.
[0051] Use concentrated sulfuric acid with a mass fraction of 98% to prepare 120mL of a sulfuric acid solution with a concentration of 300g / L, add 20g of roasted slag under the condition of a stirring speed of 90r / min to obtain a mixed solution, and keep the temperature at 80°C for 4 hours in a ...
Embodiment 2
[0055] Dry the acid mud and crush it to 160 mesh. The main components in the acid mud are calculated as (%) by mass percentage: Pb37.40, Se40.74, As3.14, Hg. Take by weighing lime powder 61g, add 50% lime powder in the selenium acid mud of 50g above-mentioned composition, mix well, place in the muffle furnace after remaining lime content is covered on the mixed material surface, control roasting temperature is 700 ℃, roasting time 10h, after reaching the reaction time and weighing after cooling, the mercury removal slag weighs 112.59g, and its main components are calculated as mass percentages (%): Se18.09, As1.36, Hg<0.02; Se, Hg , As volatilization rates were 0, 99%, 2.46%.
[0056] Use concentrated sulfuric acid with a mass fraction of 98% to prepare 200mL of a sulfuric acid solution with a concentration of 324g / L, add 20g of mercury removal slag at a stirring speed of 100r / min to obtain a mixed solution, and keep the temperature at 80°C for reaction in a water bath 6h, du...
Embodiment example 3
[0060] Dry the acid mud and crush it to 200 meshes. The main components in the acid mud are (%): Pb37.40, Se40.74, As3.14, Hg. Take by weighing lime powder 35g, add 60% lime powder in the selenium acid mud of 50g above-mentioned composition, mix well, place in the muffle furnace after remaining lime content is covered on the mixed material surface, control roasting temperature is 850 ℃, roasting time 12h, after reaching the reaction time and weighing after cooling, the mercury-removed slag weighed 82.4g, and its main components were calculated as mass percentages (%): Se24.7, A1.86, Hg0.013; Se, Hg , As volatilization rates were 0, 99%, 2.44%.
[0061] Use concentrated sulfuric acid with a mass fraction of 98% to prepare 120mL of a sulfuric acid solution with a concentration of 400g / L, add 20g of mercury removal slag at a stirring speed of 120r / min to obtain a mixed solution, and keep the temperature at 85°C for reaction in a water bath 5h, during the leaching process, add ni...
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