Method for treating nickel-containing laterite by microwave reducing roasting-goethite precipitation conversion method
A technology of precipitation conversion and nickel laterite ore, which is applied in the direction of improving process efficiency, etc., can solve problems such as equipment fouling problems, technical conditions that cannot be processed in large quantities, and thermodynamic instability of leaching slag, etc., so as to reduce the complexity of equipment , the effect of easing the operating conditions and slowing down the scaling problem
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Embodiment 1
[0027] Select different types of reducing agents such as activated carbon, charcoal, bituminous coal and anthracite, mix them with laterite ore, and place them under microwave heating at a frequency of 2450±50MHz for reduction roasting, and then leaching the calcined sand by the goethite precipitation conversion method. The nickel and cobalt in the laterite enter the leach solution, and the iron is converted into goethite precipitation. During leaching, the temperature is controlled at 90°C. Since the boiling point of the solution is not exceeded, it can be carried out in a non-closed system under normal pressure. The air flow rate was 1.0L / (L min), and the results after leaching for 4.0h are shown in Table 1. The leaching rate of cobalt was basically the same as that of nickel. Wherein R / O is the mass ratio of reducing agent to laterite ore (dry ore), A / O is the mass ratio of sulfuric acid to laterite ore (dry ore), and the pulp concentration is 10%.
[0028] Table 1
[002...
Embodiment 2
[0031] Activated carbon is selected as the reducing agent, and the amount added is 8.0% of the laterite ore mass. After mixing, it is placed in microwave heating at a frequency of 2450±50MHz for 15 minutes, and then the calcine is leached by the goethite precipitation conversion method in a closed autoclave. The nickel and cobalt enter the leach solution, and the iron is transformed into goethite precipitates. During conversion leaching, the temperature was controlled at 90°C, and pure oxygen was introduced as an oxidizing agent. The results after leaching for 2 hours are shown in Table 2. The leaching rate of cobalt is basically the same as that of nickel. Wherein A / O is the mass ratio of sulfuric acid to laterite ore (dry ore), and the pulp concentration is 10%.
[0032] Table 2
[0033]
Embodiment 3
[0035] Activated carbon is selected as the reducing agent, and the amount added is 20.0% of the mass of laterite ore. After mixing, it is placed in microwave heating at a frequency of 916±18MHz for 15 minutes. The nickel and cobalt enter the leach solution, and the iron is transformed into goethite precipitates. During conversion leaching, the mass ratio of sulfuric acid to ore (dry ore) was controlled to be 0.25, oxygen-enriched air was introduced as an oxidant, and the pulp concentration was 10%. The results after conversion and leaching for 3 hours are shown in Table 3. The leaching rate of cobalt is basically the same as that of nickel.
[0036] Table 2
[0037] temperature
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