Method of recovering vanadium from non-blast furnace titanium slag
A non-blast furnace, titanium slag technology, applied in the field of direct reduction of titanium slag to recover vanadium, can solve the problems of waste of vanadium resources, low recovery rate of vanadium, limited exploration, and no substantial breakthrough has been achieved, and achieves improvement of recovery rate, inhibition of dissolution, Achieve high-efficiency dissolution effect
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Embodiment 1
[0033] Get a certain direct reduction titanium slag, its main components are shown in Table 1, the proportion of the particles below 45 μm (325 mesh sieve) is finely ground to ≥90%; the finely ground titanium slag and a certain amount of titanium white waste acid Mixing and leaching, the leaching solid-to-liquid ratio (mass volume ratio) is 1:5kg / L, the leaching temperature is 130°C, the leaching time is 3h, and the oxygen partial pressure is 3atm; the mass concentration of sulfuric acid in the leaching process is 20%, and the obtained prepreg residue Send the titanium dioxide production process to produce titanium dioxide, and get the titanium dioxide waste liquid to return to use, and the obtained leaching solution uses iron powder to convert Fe 3+ Reduction; use the kerosene mixed solvent of P204 and TBP to extract, and the stripping agent is H 2 SO 4 ; Obtain vanadium-containing solution and prepare it into ammonium vanadate or vanadium pentoxide. The recovery rate of va...
Embodiment 2
[0035] Get a certain direct reduction titanium slag, its main components are shown in Table 1, the proportion of the particles below 45 μm (325 mesh sieve) is finely ground to ≥90%; the finely ground titanium slag and a certain amount of titanium white waste acid Mixing for leaching, the leaching solid-to-liquid ratio (mass volume ratio) is 1:4kg / L, the leaching temperature is 140°C, the leaching time is 3h, and the oxygen partial pressure is 3atm; the mass concentration of sulfuric acid in the leaching process is 22%, and the leaching aid is 20% Calcium fluoride; the obtained prepreg slag is sent to the titanium dioxide production process to produce titanium dioxide, and the titanium dioxide waste liquid is obtained for return use, and the obtained leachate is used to dilute Fe 3+ Reduction; use P507 and TBP kerosene mixed solvent for extraction, the stripping agent is HCl; obtain a vanadium-containing solution and prepare it into ammonium vanadate or vanadium pentoxide. The ...
Embodiment 3
[0037] Get a certain direct reduction titanium slag, its main components are shown in Table 1, the proportion of the particles below 45 μm (325 mesh sieve) is finely ground to ≥90%; the finely ground titanium slag and a certain amount of titanium white waste acid Mixing and leaching, the leaching solid-to-liquid ratio (mass volume ratio) is 1:3kg / L, leaching temperature is 150°C, leaching time is 3h, oxygen partial pressure is 3atm; the mass concentration of sulfuric acid in the leaching process is 25%; the obtained prepreg slag is sent to The titanium dioxide production process produces titanium dioxide, and the obtained titanium dioxide waste liquid is returned to use, and the obtained leaching solution uses sodium sulfite to dilute Fe 3+ Reduction; use the kerosene mixed solvent of P204 and TBP to extract, and the stripping agent is H 2 SO 4 ; Obtain vanadium-containing solution and prepare it into ammonium vanadate or vanadium pentoxide. The recovery rate of vanadium in ...
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