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Method for treating nickel-containing laterite by microwave reducing roasting-hematite precipitation conversion method

A technology of precipitation conversion and nickel laterite ore, applied in the direction of improving process efficiency, etc., can solve problems such as complex equipment, environmental hazards, and harsh operating conditions, and achieve the effect of slowing down scaling problems, less sulfate content, and mild operating conditions

Inactive Publication Date: 2009-03-25
NORTHEASTERN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] 1. When the temperature is in the range of 250-270°C, the pressure is as high as 3.9-5.4MPa, which puts forward high requirements on the sealing of equipment such as the sealing of mechanical stirring shaft sleeves; considering the problem of anti-corrosion, it is necessary to use an autoclave lined with titanium, so the whole set Huge investment in system equipment and harsh operating conditions
[0013] 2. When leaching in the temperature range of 250-270°C, not only the stability of ferric sulfate decreases, but also the stability of aluminum sulfate decreases
The leaching residue contains relatively high sulfate radicals (often above 10-15%), is thermodynamically unstable, and the current technical conditions cannot be processed in large quantities, so long-term storage will cause harm to the environment
[0015] In summary, there are still great difficulties in the treatment of nickel-containing laterite ore by wet process: the equipment for leaching with sulfuric acid at atmospheric pressure is simple, but the consumption of acid and alkali reagents is large; the energy consumption of the Caron process is relatively high, and the recovery rate of nickel and cobalt is low; Acid leaching can achieve a high leaching rate of nickel and cobalt under the condition of effectively reducing acid consumption. The technology is advanced, but the equipment is complicated and the investment is huge. At the same time, the scaling problem of equipment in production and the treatment of leaching residue are currently difficult to solve

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Select different types of reducing agents such as activated carbon, charcoal, bituminous coal and anthracite, mix them with laterite ore respectively, heat them under microwave at 2450±50MHz, and carry out reduction roasting. The hematite precipitation conversion method is used for leaching, nickel and cobalt enter the leaching solution, and iron is converted into hematite precipitation. The leaching temperature was controlled at 180°C, oxygen-enriched air with an oxygen volume fraction of 80% was introduced as an oxidant, and a calculated amount of 98% concentrated sulfuric acid was added. After leaching for 120 minutes, the results are shown in Table 1. The leaching rate of cobalt is 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%.

[0032] Table 1

[0033]

[0034] activated carbon 0....

Embodiment 2

[0036] Activated carbon is selected as the reducing agent, and the addition amount is 8.0% of the laterite mass. After mixing, it is heated in a microwave with a frequency of 916±18MHz for 15 minutes. Entering the leachate, the iron is converted to hematite precipitate. During conversion leaching, pure oxygen was introduced as an oxidant, and the oxygen partial pressure was controlled to 1.0 MPa. The results after leaching for 180 minutes 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 acid to laterite ore (dry ore), and the pulp concentration is 10%.

[0037] Table 2

[0038] temperature

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PUM

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Abstract

The invention relates to a method for processing laterite ore comprising nickel by means of microwave reduction roasting-hematite deposit transformation, which is characterized in that the method comprises the following steps: (1) a carbonaceous reducing agent is added into the laterite ore, and heated for 5min to 20min under microwave radiation after even blending so as to obtain laterite ore calcine; and (2) the laterite ore calcine is leached in a high-pressure container. The concentration of ore slurry leached is 10 percent to 30 percent, and the ore slurry is fed into oxygen-enriched air or pure oxygen to carry out oxidation leaching reaction. Nickel cobalt in the laterite ore enters the leached liquid, with iron transformed to hematite deposit. The method consumes less acid, with the leaching temperature greatly lower than that of the existing high-pressure acid leaching method, thereby being favorable to the decrease in manufacturing cost of leaching equipment; simultaneously, the scale in equipment is greatly decreased, the content of sulfate radical in the leaching residue is accordingly lowered, thus being favorable to the comprehensive utilization of the leaching residue.

Description

technical field [0001] The invention belongs to the technical field of mineral extraction and metallurgy. Specifically, the invention relates to a method for treating nickel-containing laterite ore by a microwave reduction roasting-hematite precipitation transformation method. Background technique [0002] Nickel is a versatile metal, often used in the production of stainless steel, superalloys, electroplating, catalysts and magnets. [0003] Although nickel exists in many kinds of minerals, there are currently two kinds of mineral raw materials for large-scale smelting and extraction of nickel, sulfide ore and oxide ore. Sulphide ore can generally be obtained by beneficiation of nickel concentrate. However, for nickel-containing oxide ores such as laterite ores, due to the different origins of the minerals, nickel and cobalt exist in the minerals in the form of lattice replacement, which are highly dispersed and cannot be enriched by direct beneficiation. Only direct chemi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B1/02C22B3/08C22B23/00
CPCY02P10/20
Inventor 翟秀静符岩畅永锋李斌川
Owner NORTHEASTERN UNIV
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