A method for efficiently recovering zinc and iron from materials containing zinc ferrite
A technology of material and acid zinc, which is applied in the field of recycling valuable metals and efficiently recovering zinc and iron, can solve the problems of incomplete volatilization, high energy consumption, and low zinc leaching rate, and achieve improved utilization, simple process flow, and low cost. low effect
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Embodiment 1
[0031] Table 1 Phase analysis of a certain zinc ferrite material
[0032]
[0033] process such as figure 1 As shown, 100g of a zinc ferrite-containing material (Zn 15.16%, Fe 30.01%, see Table 1 for phase analysis) was ground to a particle size of -200 mesh to -400 mesh, and concentrated sulfuric acid (content 98%) 50g, Sodium sulfate 10g is batched and mixed evenly, put into a muffle furnace for roasting, the roasting temperature is controlled at 200°C, and the roasting time is 2h. After roasting, place the obtained calcined sand in water for stirring and leaching, the stirring speed is 200-300rpm, the solid-to-liquid ratio (g / mL) is 1:5, and after stirring for 1 hour at 50°C, filter to obtain a zinc-iron solution and leach residue. The zinc-containing iron solution uses hydrogen peroxide as the oxidant and sodium carbonate as the pH regulator to remove iron from goethite at 40°C; after iron removal, goethite slag and zinc-containing solution are obtained; the zinc-cont...
Embodiment 2
[0036] process such as figure 1 As shown, 100g of a zinc ferrite-containing material (Zn 15.16%, Fe 30.01%, see Table 1 for phase analysis) was ground to a particle size of -200 mesh to -400 mesh, and concentrated sulfuric acid (content 98%) 40g, Potassium sulfate 15g is batched and mixed evenly, put into a muffle furnace for roasting, the roasting temperature is controlled at 250°C, and the roasting time is 2h. After roasting, place the obtained calcined sand in water for stirring and leaching, the stirring speed is 200-300rpm, the solid-to-liquid ratio (g / mL) is 1:5, and after stirring for 1 hour at 40°C, filter to obtain a zinc-iron solution and leach residue. The zinc-containing iron solution uses hydrogen peroxide as the oxidant and potassium carbonate as the pH regulator to remove iron from goethite at 50°C; after iron removal, goethite slag and zinc-containing solution are obtained; the zinc-containing solution is extracted and recovered for zinc, and extracted The ag...
Embodiment 3
[0039] process such asfigure 1 As shown, 100g of a zinc ferrite-containing material (Zn 15.16%, Fe 30.01%, see Table 1 for phase analysis) was ground to a particle size of -200 mesh to -400 mesh, and concentrated sulfuric acid (content 98%) 40g, 20g of ammonium sulfate was prepared and mixed evenly, and put into a muffle furnace for roasting, the roasting temperature was controlled at 300°C, and the roasting time was 2h. After roasting, place the obtained calcined sand in water for stirring and leaching, the stirring speed is 200-300rpm, the solid-to-liquid ratio (g / mL) is 1:5, and after stirring for 1 hour at 40°C, filter to obtain a zinc-iron solution and leach residue. The zinc-containing iron solution uses hydrogen peroxide as the oxidant and ammonium carbonate as the pH adjuster to remove iron from goethite at 70°C; after iron removal, goethite slag and zinc-containing solution are obtained; the zinc-containing solution is extracted and recovered for zinc, and extracted ...
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