Method for separating and recycling chromium from vanadium contained chromate solution
A technology for separation and recovery of vanadium-containing chromate, applied in the field of chemical metallurgy, can solve the problems of complex process, difficult implementation, and great resin damage, and achieve the effects of high metal recovery rate, reduced production cost, and low production cost.
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Embodiment 1
[0030] Take 1.5m of vanadium slag clinker water immersion solution containing V 25.3g / L and Cr 3.1g / L with a pH of 8.3 3 , add calcium oxide according to 1.3 times the stoichiometric number of vanadium forming calcium vanadate, stir and ball mill at room temperature for 2 hours, filter to obtain vanadium-precipitated liquid containing V 0.03g / L and vanadium-enriched slag containing Cr﹤0.05%. The vanadium-enriched slag is used as the raw material for the production of vanadium pentoxide, and the obtained vanadium is deposited and then liquid passes through CO 2 After adjusting the pH to 7.5, add lead carbonate according to 1.2 times of the theoretical amount of lead chromate formed by chromium, stir and ball mill at room temperature for 1.5 hours, filter the chromium-precipitated solution and chromium-enriched slag, and obtain the chromium-precipitated solution after cyclic electrodialysis , to obtain concentrated water (concentrated solution) with a conductivity of 57800 μS / cm...
Embodiment 2
[0032] Take pH 1.8 containing V 1.1g / L, Cr 2.8g / L after hydrolysis vanadium precipitation 1.5m 3, according to wherein vanadium forms ferric vanadate stoichiometric number 3 times and stirs and adds ferric sulfate, adds sodium carbonate and adjusts pH to 7.5, after 90 ℃ of reaction 2h, filter and remove wherein V, then the lead sulfate that embodiment 1 obtains is added into The filtrate was stirred and ball-milled at room temperature for 2.5 hours, and the chromium-precipitated liquid and chromium-enriched residue were obtained by filtration. The chromium-precipitated liquid is crystallized at 0°C to precipitate Glauber’s salt, and then returns to the vanadium slag clinker leaching process to continue to use. The chromium-enriched slag is stirred into the sulfuric acid-sodium sulfate solution at a solid-to-liquid ratio of 1:2g / ml, and the pH value of the solution is maintained at 85°C. 2 to 3, until the precipitate is completely converted into white, filter to obtain lead sul...
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