Fayalite type furnace slag resource recycling method
A resource recovery and fayalite technology, applied in the field of mineral engineering, can solve the problems of secondary slag, low iron recovery rate, and difficulty in taking into account the recovery of silicon resources, etc., to achieve high-efficiency separation, low cost, and resource utilization.
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[0047] The main chemical components of the copper slag and nickel slag used in this embodiment are shown in Table 1.
[0048] The chemical composition (wt.%) of table 1 copper slag and nickel slag
[0049]
specific Embodiment approach 1
[0051] Step S1, carry out ore blending with silicon oxide molar ratio 1:1 in sodium carbonate and copper slag, add carbon powder during ore blending, the addition amount of carbon powder at this moment is that iron oxide is reduced to 200% of the theoretical amount of metal iron, obtains Raw material;
[0052] Step S2, reducing and roasting the mixed raw meal at 1100° C. for 60 minutes to completely decompose ferrous silicate into metallic iron and sodium silicate. At this time, the content of zinc in the roasted clinker is 0.04%;
[0053] Step S3, the calcined clinker is ground to a particle size of d0.5≤39 μm, and leached in water at a leaching temperature of 90° C., a liquid-solid ratio of 5:1, and an leaching time of 120 minutes.
[0054] Step S4, performing solid-liquid separation on the leached pulp to obtain sodium silicate solution and leaching slag; under the conditions of the above step S3, the dissolution rate of silicon oxide is 88.5%;
[0055] Step S5, carboniz...
specific Embodiment approach 2
[0057] Step S1, carry out ore blending with silicon oxide molar ratio 1:3 in sodium carbonate and copper slag, add carbon powder during ore blending, the addition amount of carbon powder at this moment is that iron oxide is reduced to 150% of the theoretical amount of metal iron, obtains Raw material;
[0058] Step S2, reducing and roasting the mixed raw meal at 1000° C. for 60 minutes to completely decompose ferrous silicate into metallic iron and sodium silicate. At this time, the content of zinc in the roasted clinker is 0.03%;
[0059] Step S3, the calcined clinker is ground to a particle size of d0.5≤39 μm, and leached in water at a leaching temperature of 80° C., a liquid-solid ratio of 3:1, and an leaching time of 60 minutes.
[0060] Step S4, performing solid-liquid separation on the leached pulp to obtain sodium silicate solution and leaching slag; under the conditions of the above step S3, the dissolution rate of silicon oxide is 86.85%;
[0061] Step S5, carboniz...
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