Method for comprehensively utilizing vanadium slag
A vanadium slag and leaching slag technology, applied in the field of comprehensive utilization of vanadium slag, can solve the problems of large industrial waste gas, large material consumption, long process flow, etc., achieve reduced material consumption, high comprehensive yield, and shortened process flow Effect
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[0035] C, the preparation of vanadium-containing solution: the extract is carried out back extraction, and the lower clear liquid is the vanadium-containing solution; wherein, the stripping agent is the sulfuric acid of 50~300g / L, and stripping ratio (O / A)=(2 ~10): 1;
[0036]d. Preparation of electrolytic manganese: After adjusting the pH value of the raffinate obtained in step b to 4.0-6.0, add ammonium sulfate and trace selenium dioxide for electrolysis to obtain electrolytic manganese; wherein, the electrolytic current density is 100-300A / m -2 , electrolysis temperature 20~50℃; ammonium sulfate concentration 80~150g / L;
[0037] e, preparation of titanium dioxide: adding sulfuric acid to the leaching slag obtained in step a, carrying out secondary acid leaching, filtering to obtain a secondary leaching solution; heating the secondary leaching solution, adding Fe 3+ reduced to Fe 2+ , freeze to make ferrous sulfate crystallize, filter to obtain titanyl sulfate, hydrolyze...
Embodiment 1
[0050] Embodiment 1 Utilize the method of the present invention to reclaim vanadium, titanium, manganese in vanadium slag
[0051] (1) Oxygen pressure acid leaching:
[0052] Crush the vanadium slag, ball mill, take 100g of converter vanadium slag with a particle size of -0.075~+0.055mm (-200~+260 mesh), add it to a sulfuric acid solution with an initial acid concentration of 200g / L, and calculate the volume of sulfuric acid: the mass of converter vanadium slag The ratio (liquid-solid ratio) is 10:1, the acid leaching time is 90min, the stirring speed is 500rpm, the acid leaching temperature is 90°C, and oxygen is maintained during the acid leaching process, and the oxygen pressure is 0.5MPa. Liquid-solid separation is carried out after leaching, the leaching solution is the leaching solution containing vanadium acid, and the leaching residue is the leaching residue enriched in titanium. Under these conditions, the leaching rate of vanadium is 64.33%, and that of titanium is ...
Embodiment 2
[0060] Embodiment 2 Utilize the method of the present invention to recover vanadium, titanium, manganese in vanadium slag
[0061] (1) Oxygen pressure acid leaching:
[0062] Crush the vanadium slag, ball mill, take 100g of converter vanadium slag with a particle size of -0.075~+0.055mm (-200~+260 mesh), add it to a sulfuric acid solution with an initial acid concentration of 200g / L, and calculate the volume of sulfuric acid: the mass of converter vanadium slag The ratio (liquid-solid ratio) is 10:1, the acid leaching time is 90min, the stirring rate is 500rpm, the acid leaching temperature is 160°C, the oxygen flow is maintained during the acid leaching process, and the oxygen pressure is 0.5MPa. Liquid-solid separation is carried out after leaching, the leaching solution is the leaching solution containing vanadium acid, and the leaching residue is the leaching residue enriched in titanium. Under this condition, the leaching rate of vanadium was 98.37%, that of titanium was...
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