Clean manufacturing technique of extracting vanadium pentoxide from vanadium-contained stone coal
A vanadium pentoxide and clean production technology, which is applied in the field of clean production technology for extracting vanadium pentoxide, can solve the problems of inconvenient operation and difficult promotion and use, and achieve high leaching rate and recovery rate
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Embodiment 1
[0010] Example 1 takes V 2 O 5 A grade of 1.05% vanadium-containing rock ore, crush the quarry to a particle size of less than 2mm, sample 2000g and roast in an industrial microwave equipment, roasting temperature 700℃, roasting time 1h; after roasting, finely grind the clinker to 100% less than 0.15 mm, add water to make a slurry, make the liquid-solid ratio (volume to mass ratio) 1.5:1, add sulfuric acid for leaching of vanadium pentoxide, the amount of sulfuric acid is 22% of the mass of the stone coal, the leaching process temperature is 95℃, and the leaching time is 6h , V 2 O 5 The leaching rate can reach 83.5%. The leaching solution is reduced by iron powder to ferric ions, adjusted to pH 2.8-3.0 with lime and ammonia, and then extracted by solvent, oxidized, and added with ammonia to obtain ammonium polyvanadate precipitation, which is calcined to prepare powder V 2 O 5 Product, V 2 O 5 The recovery rate was 76.50%.
Embodiment 2
[0011] Example 2 Take V 2 O 5 The vanadium-containing ore with a grade of 0.87%, the quarry is pulverized to a particle size of less than 2mm, and 2000g is sampled and roasted in an industrial microwave equipment. The roasting temperature is 750℃ and the roasting time is 1.5h; after roasting, the clinker is finely ground to 100% less than 0.15mm, add water to make a slurry, make the liquid-solid ratio (volume to mass ratio) 1:1, add sulfuric acid to leaching vanadium pentoxide, the amount of sulfuric acid is 24% of the mass of the stone coal, the leaching process temperature is 95℃, and the leaching time 8h, V 2 O 5 The leaching rate can reach 82.0%. The leaching solution is reduced with iron powder to ferric ions, adjusted to pH 2.8-3.0 with lime and ammonia, and then extracted with solvent, oxidized, and added with ammonia to obtain ammonium polyvanadate precipitation, and ammonium polyvanadate is calcined to prepare powder V 2 O 5 Product, V 2 O 5 The recovery rate was 75.0%....
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