Method for volatilizing and enriching molybdenum from molybdenum tailings
A molybdenum tailings and enrichment technology, applied in the field of solid waste recycling, can solve problems such as limitations and no relevant research reports on enrichment and recovery, and achieve the effects of reducing production costs and solving hidden dangers of sand and dust pollution and debris flow
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Embodiment 1
[0025] Huludao molybdenum tailings are used, and the main phase of the tailings is SiO 2 , the molybdenum content is 0.19%, the tailings are ball milled to a particle size within the range of 0.08-0.1mm, and water is added to stir, so that the molybdenum tailings form a molybdenum tailings slurry with a certain rheological property with a water content of 30%-40% WT , in order to better contact and react with acid. Then add 0.25mlHF (hydrofluoric acid) metering according to every gram of dry base molybdenum tailings, the concentration of this HF is 40%WT, after the reaction bubble disappears, add HCl (hydrochloric acid), the concentration of HCl is 36%WT, the addition of hydrochloric acid The amount is 0.25ml HCl / g dry molybdenum tailings. After adding acid, cover and heat at 250°C for 40 minutes, remove the cover after heat treatment, and dry at 65°C until the mass change is less than 5%. The pretreated molybdenum tailings are heated by HF-HCl and heat-treated at 900°C to m...
Embodiment 2
[0027] Except that the added amount of hydrochloric acid is 1ml HCl / g dry base molybdenum tailings, the others are the same as in Example 1, and the high-temperature volatilization rate of molybdenum can reach 98.6% at 900°C.
Embodiment 3
[0029] Except that the addition of hydrofluoric acid is 0.625ml / g dry base molybdenum tailings, and the addition of hydrochloric acid is 0.625ml / g dry base molybdenum tailings, the rest are the same as in Example 1, and the high temperature volatility of molybdenum at 900°C can be Reached 85.8%.
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