Method for recycling vanadium, chromium, titanium and iron from vanadium-titanium magnetite ore
A technology for vanadium-titanium magnetite and vanadium-titanium-magnetite, which is applied in the fields of iron, chromium, high-titanium chromium-type vanadium-titanium magnetite or concentrate for comprehensive recovery and utilization of vanadium and titanium, can solve the problem of inability to extract chromium and the like, and achieves the Conducive to the leaching rate, economical, and the effect of improving the recovery rate
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Embodiment 1
[0036] Grind Panzhihua Hongge vanadium-titanium magnetite iron concentrate to powder, wherein -200 mesh accounts for 80%, and the concentrate contains (weight percent, %wt): TFe56.7, TiO 2 12.9, V 2 o 5 0.58, Cr 2 o 3 1.11, take 1000g of ground concentrate, add 80g of sodium carbonate, 20g of sodium nitrate, oxidize and roast in the rotary kiln at 900°C-1000°C for 2.5-3 hours, and leaching the clinker with hot water at 80°C, the liquid-solid ratio is 5 : 1, the leaching solution after purification is precipitated by the ammonium salt vanadium precipitation method to produce ammonium polyvanadate, and after calcining, vanadium pentoxide is obtained; the recovery rate of vanadium is 83%. After vanadium precipitation, the raffinate is reduced with sodium sulfide, the pH value is adjusted to be alkaline, chromium hydroxide is precipitated, and chromium trioxide is obtained after calcining, and the recovery rate of chromium is 76%. The weight of leaching residue is 1050g, conta...
Embodiment 2
[0038] Grinding Panzhihua Hongge vanadium-titanium magnetite iron concentrate to -200 mesh accounts for 70%, and the concentrate contains (weight percent, %wt): TFe55.2, TiO 2 13.1,V 2 o 5 0.58, Cr 2 o 3 0.87, take 10Kg of ground concentrate, add 0.9Kg of sodium carbonate, 0.1Kg of sodium nitrate, oxidize and roast in a rotary kiln at 1000-1100°C for 2 hours, clinker is leached with hot water at 70°C, and the liquid-solid ratio is 5: 1. Precipitate ammonium polyvanadate from the purified leaching solution by ammonium salt vanadium precipitation method, and obtain vanadium pentoxide after calcination; the recovery rate of vanadium is 84.5%. After vanadium precipitation, the raffinate is reduced with sodium sulfide, the pH value is adjusted to be alkaline, chromium hydroxide is precipitated, and chromium trioxide is obtained after calcining, and the chromium recovery rate is 77.5%. The weight of leaching residue is 10.7Kg, containing TFe53.5%, TiO 2 13.0%, Na 2 O2.3%. The...
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