Cleaning and smelting process for low-grade complex nickel-molybdenum ore
A nickel-molybdenum ore, low-grade technology, applied in the clean smelting process of low-grade complex nickel-molybdenum ore, can solve the problems of long process, low concentration, poor environment, etc., achieve efficient separation and recovery, realize resource utilization, and reduce pollution.
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Embodiment 1
[0032] The chemical composition of nickel-molybdenum ore A is (%): Mo 5.81%, Ni 6.12%, Zn 3.19%, Fe 17.22%, As0.8%, Al 3.11%, Si 16.63%, SiO 2 22.7%, P 1.18%, S 27.9%.
[0033] First, mix 10g of nickel-molybdenum ore A with a particle size of -150 mesh, chlorinating agent, 2g of pulverized coal and 3g of water to make balls with an average particle size of 1.5mm. The chlorination agent is a mixture of ammonium chloride and calcium chloride, wherein ammonium chloride accounts for 35wt.%, and calcium chloride accounts for 65wt.%. The amount of chlorinating agent added is to convert all As, Mo, and Zn in 10g nickel-molybdenum ore A into AsCl 3 、MoCl 5 , ZnCl 2 2.5 times the required theoretical amount. Put the wet balls directly into the volatilization kiln which has been raised to 380°C for chlorination and volatilization, and keep it warm for 60 minutes. At this time, under the action of the negative pressure induced draft fan at the flue mouth of the volatilization kiln,...
Embodiment 2
[0035] The chemical composition of nickel-molybdenum ore B is (%): Mo 3.07%, Ni 6.88%, Zn 1.49%, Fe 18.6%, As0.39%, Si 13.55%, SiO 2 23.1%, P 1.53%, S 21.5%.
[0036] First, mix 100g of nickel-molybdenum ore B with a particle size of -250 mesh, chlorinating agent, 30g of pulverized coal and 20g of water to make balls with an average particle size of 2.0mm. The chlorination agent is a mixture of ammonium chloride and calcium hypochlorite, wherein ammonium chloride accounts for 60wt.%, and calcium chloride accounts for 40wt.%. The amount of chlorinating agent added is to convert As, Zn, and Mo in 100g nickel-molybdenum ore B into AsCl 3 、MoCl 5 , ZnCl 2 4 times the required theoretical amount. Put the wet pellets directly into the volatilization kiln which has been raised to 350°C for chlorination and volatilization, and keep it warm for 80 minutes. At this time, under the action of the negative pressure induced draft fan at the flue mouth of the volatilization kiln, the p...
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