Method for extracting vanadium from mixed vanadium slag and vanadium-containing steel slag through pressurization
A technology of steel slag and vanadium slag, applied in the direction of improving process efficiency, etc., can solve the problems of reducing leaching rate, high price, and loss of KOH medium, and achieve the effect of reducing energy consumption and increasing leaching rate
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Embodiment 1
[0038] Put vanadium-containing steel slag and vanadium slag mixed with vanadium raw materials into the pressure reactor, the mass ratio of vanadium-containing steel slag to vanadium slag is 1:10, and at the same time, add 20wt % NaOH solution. Seal the pressurized reaction kettle, feed oxygen and heat for leaching reaction, control oxygen partial pressure to 0.2MPa, leaching reaction temperature to 120°C, leaching reaction pressure to 0.6MPa, and reaction time to 0.5h. After the reaction, the reaction kettle is cooled to 60°C and the reaction kettle is opened, and the obtained mixed slurry is filtered and separated to obtain vanadium-containing leaching solution and tailings. The vanadium-containing leaching solution is crystallized and separated to obtain sodium vanadate product, and the separated crystallized liquid is circulated for leaching reactions.
[0039] After testing, the leaching rate of vanadium is 85%.
Embodiment 2
[0041] Put vanadium-containing steel slag and vanadium slag mixed with vanadium raw materials into the pressure reaction kettle, the mass ratio of vanadium-containing steel slag to vanadium slag is 1:8, and at the same time add 24wt % NaOH solution. Seal the pressurized reaction kettle, feed oxygen and heat for leaching reaction, control oxygen partial pressure to 0.1MPa, leaching reaction temperature to 140°C, leaching reaction pressure to 0.5MPa, and reaction time to 1.5h. After the reaction, the reaction kettle is cooled to 75°C, and the reaction kettle is opened, and the obtained mixed slurry is filtered and separated to obtain vanadium-containing leaching solution and tailings. The vanadium-containing leaching solution is crystallized and separated to obtain sodium vanadate product, and the separated liquid is circulated after crystallization for leaching reactions.
[0042] After testing, the leaching rate of vanadium is 91%.
Embodiment 3
[0044] Put vanadium-containing steel slag and vanadium slag mixed with vanadium raw materials into the pressure reactor, the mass ratio of vanadium-containing steel slag to vanadium slag is 1:6, and at the same time add 45wt % NaOH solution. Seal the pressurized reaction kettle, feed oxygen and heat for leaching reaction, control oxygen partial pressure to 0.2MPa, leaching reaction temperature to 120°C, leaching reaction pressure to 0.7MPa, and reaction time to 1.8h. After the reaction, the reaction kettle is cooled to 65°C and the reaction kettle is opened, and the obtained mixed slurry is filtered and separated to obtain vanadium-containing leaching solution and tailings. The vanadium-containing leaching solution is crystallized and separated to obtain sodium vanadate product, and the separated crystallized liquid is circulated for leaching reactions.
[0045] After testing, the leaching rate of vanadium is 95%.
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