Method for extracting valuable metals from acid leaching solution of nickel-molybdenum multi-metal metallurgical materials by separation
A multi-metal and acid leaching technology, applied in the direction of improving process efficiency, etc., can solve problems such as non-application, molybdenum loss, iron interference, etc., and achieve the effect of simple operation, low production cost and short process
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Embodiment 1
[0018] Nickel molybdenum ore oxidation roasting acid leaching solution contains Mo 8.2g / L, Ni 2.6g / L, add Na first 2 CO 3 Adjust the pH value to 1.5, and then use weak base anion exchange resin D315 to adsorb the molybdenum in it. The adsorption contact time is 50 minutes. The negative molybdenum resin is desorbed with 4.5mol / L ammonia water, and the desorption contact time is 60 minutes. Magnesium chloride is used to purify and remove P, As and Si. After purification, the liquid is deeply removed by strong base anion resin D231. After vanadium removal, nitric acid is added to the liquid to adjust the pH value to 2.0 to crystallize high-quality ammonium molybdate. After the liquid is transferred, NaHCO is added to the liquid. 3 Adjust the pH of the solution to 3.5, stir at 50°C for 1 hour, filter, and use chelating resin D412 to absorb the nickel in the filtrate. The contact time is 70 minutes. The negative nickel resin is desorbed with 1mol / L sulfuric acid. The contact time i...
Embodiment 2
[0020] Nickel-molybdenum ore calcification and oxidation roasting, low-temperature sulfate roasting, calcination and water stirring and leaching to obtain a solution containing Mo 10.5g / L, Ni 4.1g / L, and a pH value of 0.8. The leaching solution uses weak base anion exchange resin D314 to absorb molybdenum. and vanadium, the adsorption contact time is 70min, the negative molybdenum vanadium resin is desorbed with 1.5mol / L sodium hydroxide solution, the desorption contact time is 45min, the molybdenum solution is purified by magnesium sulfate to remove impurities, evaporates and crystallizes to obtain sodium molybdate, and the crystallization mother liquor is added with chloride Ammonium metavanadate is obtained by crystallization of ammonium, and CaCO is added to the solution after molybdenum extraction 3 , stirred at 80°C for 1.5 hours, adjusted the pH of the solution to 4.5, precipitated iron, aluminum, etc., filtered, then added ammonia water to adjust the pH value to 6.0 and...
Embodiment 3
[0022] The acid leaching solution for oxidation and roasting of waste petroleum catalysts contains Mo 6.5g / L, Ni 1.8g / L, adding NaOH to adjust the pH value to 0.4, and using strong base anion exchange resin D231 to adsorb molybdenum, the adsorption contact time is 90min, and it is used for negative molybdenum resin 5.5mol / L ammonia water desorption, desorption contact time 50min, after the molybdenum solution is left to settle vanadium, purify it with magnesium chloride to remove P, As and Si, and the purified solution is deeply removed by strong base anion resin D231, and the solution after vanadium removal Add nitric acid to adjust the pH value to 2.2 to crystallize ammonium molybdate, add NaHCO to the solution after molybdenum extraction 3 Adjust the pH value to 4.0, extract the nickel with P507, back-extract the loaded organic phase with nitric acid, evaporate, concentrate and crystallize the back-extracted solution to obtain industrial nickel nitrate. The total recovery r...
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