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 problems such as difficult popularization and use, and inconvenient operation
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Embodiment 1
[0009] Example 1 Take V 2 o 5 Vanadium-containing stone coal ore with a grade of 1.05%, crush the stone coal ore to a particle size of less than 2mm, sample 2000g and roast it in industrial microwave equipment at a roasting temperature of 700°C for 1 hour; after roasting, finely grind the clinker until 100% is less than 0.15 mm, add water to make slurry, make the liquid-solid ratio (volume to mass ratio) 1.5:1, add sulfuric acid to carry out vanadium pentoxide leaching, the amount of sulfuric acid is 22% of the stone coal ore quality, the temperature of the leaching process is 95 ℃, and the leaching time is 6h , V 2 o 5 The leaching rate can reach 83.5%. Iron powder is used to reduce ferric ions in the leachate, and the pH value is adjusted to 2.8-3.0 with lime and ammonia water. After solvent extraction, oxidation, and ammonia water are added, ammonium polyvanadate is precipitated, and ammonium polyvanadate is calcined to prepare powder V 2 o 5 product, V 2 o 5 The rec...
Embodiment 2
[0010] Example 2 Take V 2 o 5 For vanadium-containing stone coal ore with a grade of 0.87%, the stone coal ore is crushed to a particle size of less than 2mm, and a sample of 2000g is roasted in industrial microwave equipment at a roasting temperature of 750°C for 1.5 hours; after roasting, the clinker is finely ground to 100% less than 0.15mm, add water to make slurry, make the liquid-solid ratio (volume to mass ratio) 1:1, add sulfuric acid to carry out vanadium pentoxide leaching, sulfuric acid dosage is 24% of stone coal ore quality, leaching process temperature 95 ℃, leaching time 8h, V 2 o 5 The leaching rate can reach 82.0%. Iron powder is used to reduce ferric ions in the leachate, and the pH value is adjusted to 2.8-3.0 with lime and ammonia water. After solvent extraction, oxidation, and ammonia water are added, ammonium polyvanadate is precipitated, 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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