Method for preparing magnesium hydrate nano powder by active acid leaching nickel-containing serpentine
A technology of magnesium hydroxide and nano-powder, applied in magnesium hydroxide and other directions, can solve the problems of increased purification and impurity removal costs, high acidity of leaching solution, and high leaching cost, and achieves shortened preparation cycle, good product quality, and shortened reaction time. Effect
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Embodiment 1
[0015] Example 1: Take the serpentine ore containing 0.5-1% nickel, 25% MgO, and 1.72% Mn and heat it at 550°C for 1.5h for activation pretreatment. After taking it out, ball mill it to -74 μm, and then add 3.0mol / L sulfuric acid was leached in the microwave for 30min, the solid-liquid ratio was 1:8, the leaching temperature was 100°C, the stirring speed was 900r / min, the pH value of the leaching solution was 1.8, and then Na with a concentration of 7.2mol / L was added. 2 CO 3 The solution is filtered until the pH is 2 to remove iron, and the leaching solution after sinking alum is added with Na at a concentration of 2.5mol / L at 40°C. 2 S solution until the pH is 5.2. At this time, the heavy metal ions in the leaching solution form black precipitates. Filter the purified solution obtained by filtering the precipitates. Add sodium hydroxide with a concentration of 5.0 mol / L under the condition of constant stirring speed at 30 ° C. The pH of the solution is 7.3 for nickel preci...
Embodiment 2
[0016] Example 2: Take the serpentine ore containing 1% nickel, 28% MgO, and 1.52% Mn and heat it at 550°C for 1.5h for activation pretreatment. After taking it out, it will be ball milled to -74 μm, and then the solid-to-liquid ratio will be 1. :7 Add 3.5mol / L sulfuric acid for conventional leaching for 2 hours, the leaching temperature is controlled at 100°C, the stirring speed is 900r / min, the pH value of the leaching solution is 1.8, and then adding Na concentration of 7.5mol / L 2 CO 3 The solution is filtered until the pH is 2 to remove iron; the leaching solution after iron removal is stirred at 45°C and 900r / min, and Na with a concentration of 2.5mol / L is added. 2 S solution until the pH is 5.1. At this time, the heavy metal ions in the leaching solution form black precipitates. Filter the purified solution from the precipitates at 35°C and add a sodium hydroxide solution with a concentration of 5.5 mol / L under the condition of constant stirring speed. When the pH is 7....
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