Method for extracting vanadium from vanadium containing material
A material and clinker technology, applied in the field of vanadium slag hydrometallurgy and vanadium chemical industry, can solve the problems of waste and increase production cost, and achieve the effect of saving consumption, reducing consumption and efficient extraction
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Embodiment 1
[0063] (1) Put V 2 o 5 The vanadium-titanium magnetite with a content of 15% is roasted at 850°C;
[0064] (2) After the roasted clinker obtained in step (1) is treated by a waste heat recovery device, the temperature is reduced to 200 ° C, and then the clinker is crushed by wet ball milling, so that the proportion of the clinker with a particle size of -100 mesh is 70%, and filtered Finally, the moisture content of the clinker is 20%;
[0065] (3) ammonium bicarbonate and the clinker obtained after step (2) are filtered prepare reaction mass by the mass ratio of 1:10, add the stearic acid of 0.5wt% in reaction mass simultaneously;
[0066] (4) Add the reaction materials into the drum reactor, raise it to 45° C. for 1 hour at a rate of 1.5° C. / min, and control the rotating speed of the reactor to be 8 r / min;
[0067] (5) Place the ammonified material obtained in step (4) in a drum reactor with a pressure of -100pa, raise the temperature to 80°C at a rate of 1°C / min and keep...
Embodiment 2
[0071] (1) Put V 2 o 5 The vanadium-titanium magnetite with a content of 15% is roasted at 880°C;
[0072] (2) After the roasted clinker obtained in step (1) is treated by a waste heat recovery device, the temperature is reduced to 230° C., and then the clinker is crushed by wet ball milling, so that the proportion of the clinker with a particle size of -100 mesh is 73%, and filtered Finally, the moisture content of the clinker is 23%;
[0073] (3) ammonium carbonate and the clinker obtained after step (2) are filtered prepare reaction mass by the mass ratio of 1:5, add the stearic acid of 0.6wt% in reaction mass simultaneously;
[0074] (4) Put the reaction materials into the drum reactor, raise it to 47°C at a rate of 1.5°C / min and keep it warm for 1.2h, and control the rotational speed of the reactor to be 10r / min;
[0075] (5) Place the ammonified material obtained in step (4) in a drum reactor with a pressure of -130pa, raise the temperature to 85°C for 2.5h at a rate ...
Embodiment 3
[0079] (1) Put V 2 o 5 Vanadium-titanium magnetite with a content of 17% is roasted at 900°C;
[0080] (2) After the roasted clinker obtained in step (1) is treated by a waste heat recovery device, the temperature is reduced to 250° C., and then the clinker is crushed by wet ball milling so that the proportion of the clinker with a particle size of -100 mesh is 75%, and filtered Finally, the moisture content of the clinker is 25%;
[0081] (3) Ammonium bicarbonate and the clinker obtained after step (2) are filtered prepare reaction mass by the mass ratio of 1:4, add the stearic acid of 0.7wt% in reaction mass simultaneously;
[0082] (4) Put the reaction materials into the drum reactor, raise it to 40° C. for 1.5 hours at a rate of 1.2° C. / min, and control the rotational speed of the reactor to be 12 r / min;
[0083] (5) Place the ammonified material obtained in step (4) in a drum reactor with a pressure of -200pa, raise the temperature to 90°C at a rate of 1.5°C / min and ke...
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