Method for extracting vanadium and removing arsenic from arsenic-containing waste sulfuric acid catalyst
A catalyst and sulfuric acid technology, applied in the field of hydrometallurgy, can solve the problems of high energy consumption, ferric sulfate crusting, and high production cost, and achieve the effects of simple process flow, efficient and clean extraction, and short reaction time.
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Embodiment 1
[0030] 1) Mix the arsenic-containing waste sulfuric acid catalyst ball-milled to 100 μm with a 10% sodium hydroxide solution for hydrothermal reaction. The mass ratio of the sodium hydroxide solution to the arsenic-containing waste sulfuric acid catalyst is 2:1. The reaction temperature is 80°C, the reaction time is 1h, and the stirring speed is 300r / min. The liquid-solid separation of the reacted material is carried out, and the obtained liquid phase is the leachate;
[0031] 2) Removal of arsenic in the leaching solution: add NaOH to the leaching solution to adjust the pH to 12, then add arsenic removing agent polymerized ferrous sulfate in an amount twice the molar amount of arsenic in the leaching solution, mix and stir, and filter to obtain a purified vanadium solution.
[0032] Through detection and calculation, the vanadium recovery rate in this embodiment is 82.35%, and the arsenic removal rate is 98.63%.
Embodiment 2
[0034] 1) Mix the arsenic-containing waste sulfuric acid catalyst ball-milled to 200 μm with a 15% sodium hydroxide solution for hydrothermal reaction, the mass ratio of the sodium hydroxide solution to the arsenic-containing waste sulfuric acid catalyst is 4:1, hydrothermal reaction The reaction temperature is 90°C, the reaction time is 2 hours, and the stirring speed is 500r / min. The liquid-solid separation of the reacted material is carried out, and the obtained liquid phase is the leachate;
[0035] 2) Removal of arsenic in the leaching solution: add NaOH to the leaching solution to adjust the pH to 14, then add arsenic removing agent polymerized ferric sulfate in an amount 10 times the molar amount of arsenic in the leaching solution, mix and stir, and filter to obtain a purified vanadium solution.
[0036] Through detection and calculation, the vanadium recovery rate in this embodiment is 85.68%, and the arsenic removal rate is 99.92%.
Embodiment 3
[0038] 1) Mix the arsenic-containing waste sulfuric acid catalyst ball-milled to 80 μm with 20% sodium carbonate solution for hydrothermal reaction, the mass ratio of sodium carbonate solution to the arsenic-containing waste sulfuric acid catalyst is 5:1, and the hydrothermal reaction temperature The temperature is 70°C, the reaction time is 0.5h, and the stirring speed is 200r / min. The material after the reaction is subjected to liquid-solid separation, and the obtained liquid phase is the leachate;
[0039] 2) Removing arsenic from the leaching solution: adding Na to the leaching solution 2 CO 3 Adjust the pH to 14, then add polyaluminum sulfate, an arsenic removing agent, in an amount 20 times the molar amount of arsenic in the leaching solution, mix and stir, and filter to obtain purified vanadium solution.
[0040] Through detection and calculation, the vanadium recovery rate in this embodiment is 81.23%, and the arsenic removal rate is 98.96%.
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