Clean production method in atmospheric pressure leaching of limonite type laterite-nickel ore with hydrochloric acid
A technology of laterite nickel ore and cleaner production, applied in the field of limonite type laterite nickel ore hydrochloric acid normal pressure leaching clean production, can solve the problems of high iron ion concentration and difficult separation, and achieve the effects of reducing discharge and solving difficult treatment.
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Embodiment 1
[0026] The raw material is limonite-type lateritic nickel ore. After grinding, the particle size is controlled below 200 mesh, accounting for more than 85% of the total ore. It is added to the enamel reaction kettle together with hydrochloric acid with a mass percentage concentration of 31% according to the acid ore mass ratio of 2.5:1. Mix and heat up, and start timing the reaction when the temperature reaches 100°C. After the reaction is finished, plate and frame filter press is carried out, and the main element composition in the pickling solution is: Fe 2 o 3 : 114.7g / L, Ni: 2.76g / L, Co: 0.24g / L, Cr: 3.09g / L, Al: 7.98g / L, Mg: 3.93g / L. The pickling solution is pumped into the calcining hydrolysis furnace at a flow rate of 100L / h by a metering pump, and after being atomized, the calcining reaction is carried out at 300°C. The hydrogen chloride gas generated by the reaction enters the two-stage packing absorption tower after two-stage dust removal by cyclone dust removal an...
Embodiment 2
[0028] The raw material is limonite-type lateritic nickel ore. After grinding, the particle size is controlled below 200 mesh, accounting for more than 85% of the total ore. It is added to the enamel reaction kettle together with hydrochloric acid with a mass percentage concentration of 22% according to the acid ore mass ratio of 4:1. Mix and heat up, and start timing the reaction when the temperature reaches 80°C. After the reaction is finished, plate and frame filter press is carried out, and the main element composition in the pickling solution is: Fe 2 o 3 : 120.6g / L, Ni: 3.07g / L, Co: 0.33g / L, Cr: 4.11g / L, Al: 8.02g / L, Mg: 2.97g / L. The pickling liquid is pumped into the calcining hydrolysis furnace at a flow rate of 50L / h by a metering pump, and after being atomized, the calcining reaction is carried out at 500°C. The hydrogen chloride gas generated by the reaction enters the two-stage packing absorption tower after two-stage dust removal by cyclone dust removal and bag ...
Embodiment 3
[0030] The raw material is limonite-type lateritic nickel ore. After grinding, the particle size is controlled below 200 mesh, accounting for more than 85% of the total ore. It is added to the enamel reaction kettle together with hydrochloric acid with a mass percentage concentration of 18% according to the acid ore mass ratio of 5:1. Mixing was performed, the temperature was raised, and the reaction was timed when the temperature reached 50°C. After the reaction is finished, plate and frame filter press is carried out, and the main element composition in the pickling solution is: Fe 2 o 3 : 119.3g / L, Ni: 3.55g / L, Co: 0.36g / L, Cr: 4.35g / L, Al: 8.56g / L, Mg: 3.05g / L. The pickling solution is poured into the calcining hydrolysis furnace with a metering pump at a flow rate of 1000L / h, and after being atomized, the calcining reaction is carried out at 300°C. The hydrogen chloride gas generated by the reaction enters the two-stage packing absorption tower after being dedusted by c...
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