Dearsenifying method for Cu-Zn-Co material
A material, copper and zinc technology, applied in the field of arsenic removal from copper ore smelting method and mineral pretreatment in non-ferrous metal smelting, can solve the problems of low recovery cost, high metal recovery rate, strict requirements, etc. The effect of high removal rate and low cost
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Embodiment 1
[0011] The sodium hydroxide solution is impregnated with the copper-zinc-cobalt material particles, the concentration of the sodium hydroxide solution is 120 g / liter, the mass ratio of the sodium hydroxide solution to the solid material is 5:1, the leaching time is 1 hour, and the leaching temperature is 90 degrees. Three-stage countercurrent impregnation was adopted.
[0012] The chemical components of copper, zinc and cobalt materials before impregnation: Cu 23.33%, Zn 25.91%, Co 0.87%, Fe 1.63%, As 3.81%, S 6.88%, Pb 1.69%, Cd 3.15%, Ni 0.15%, Mn 0.47 %, Bi 0.012%, Sn 0.0066%, CaO 0.86%, MgO 1.09%, Al 2 o 3 0.16%, SiO 2 3.96% and other trace ingredients.
[0013] The slag obtained after treatment with strong alkali solution contains Cu 35.48%, Zn 32.26%, Co 1.21%, Fe 1.74%, CaO 0.98%, MgO 1.05%, SiO 2 6.40%, As 0.17%, S 0.48%, Cd 4.26%, leaching rate As 97.7%, S 96%, Pb 53.8%, Zn 16.6%, this material can fully meet the new smelting needs of copper, zinc and cobalt se...
Embodiment 2
[0027] The sodium hydroxide solution is impregnated with the copper-zinc-cobalt material particles, the concentration of the sodium hydroxide solution is 160 g / liter, the mass ratio of the sodium hydroxide solution to the solid material is 3:1, the leaching time is 0.5 hour, and the leaching temperature is 95 degrees. Two-stage countercurrent impregnation was used.
[0028] The sodium hydroxide solution becomes the leaching solution after impregnating the copper, zinc and cobalt material particles. After concentrated crystallization, the mother liquor is recycled to remove the impregnation material. After the crystallization mixture is dissolved in water, it is replaced with calcium hydroxide to recover calcium arsenate, and then the mother liquor is concentrated and crystallized to produce Glauber's salt, and then the residual liquid is used to wash the leaching slag and recycled to impregnate copper, zinc and cobalt materials.
Embodiment 3
[0030] The sodium hydroxide solution is impregnated with copper, zinc and cobalt material particles, the concentration of the sodium hydroxide solution is 80 g / liter, the mass ratio of the sodium hydroxide solution to the solid material is 7:1, the leaching time is 2 hours, and the leaching temperature is 85 degrees. Four-stage countercurrent impregnation is adopted.
[0031] The sodium hydroxide solution becomes the leaching solution after impregnating the copper, zinc and cobalt material particles. After concentrated crystallization, the mother liquor is recycled to remove the impregnation material. After the crystallization mixture is dissolved in water, it is replaced with calcium hydroxide to recover calcium arsenate, and then the mother liquor is concentrated and crystallized to produce Glauber's salt, and then the residual liquid is used to wash the leaching slag and recycled to impregnate copper, zinc and cobalt materials.
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