Technology for recovering nickel, cobalt and iron from nickel oxide ores through high-temperature chlorinating volatilization

A nickel oxide ore, high-temperature chlorination technology, applied in the field of hydrometallurgy, can solve the problems of less consumption of reagents, large amount of immersion solution, complex operation process, etc., to improve the chlorination volatilization rate, be friendly to the production environment, and shorten the process The effect of the process

Inactive Publication Date: 2014-12-24
毛黎生 +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In addition, in the first step of the process, that is, during the pre-neutralization with calcium oxide or calcium hydroxide to remove iron and aluminum, precious A large loss of nickel and cobalt
[0005] A method of roasting-leaching treatment of limonite-type nickel oxide ore was previously applied for (patent application number: 201010131130.0). Compared with the existing roasting-leaching process, this method has a short flow process and less reagent consumption, and can effectively Recovering nickel and cobalt in nickel oxide ore, the leaching slag is easy to comprehensively utilize, but because the nickel oxide ore is reduced and roasted first, then cooled to 300-500 °C, and then chlorinated by the two-step process of chlorination and roasting, the equipment increase, investment increase, complex operation process, and all calcined sand needs to be leached, the amount of leaching solution is large, and the metal recovery rate is low
[0006] The high-temperature chlorination method of lateritic nickel ore (patent application number: 200910094630.9) that was first applied for, the disadvantage of this method is that the high-temperature chlorination roasting temperature used is low, and the volatilization temperature of nickel chloride is 973°C.
Therefore, nickel chloride in laterite nickel ore cannot be converted into gas and enter the flue gas recovery at high temperature.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] The composition of nickel oxide ore contains (weight%): Ni 1.45%, Fe 14.5%, C00.08%, MgO18.5%, SiO 35.7%, CaO 0.3%, Al 2 o 3 6.08%, Cr 1.02%.

[0031] The nickel oxide ore and coke powder are crushed and ball milled respectively, and the fineness of the nickel oxide ore after ball milling is 100 mesh.

[0032] Chlorination roasting conditions: add 20% calcium chloride and 0.5% coke powder according to the weight of nickel oxide ore, roasting temperature is 1250°C, and roasting time is 10 hours, so that the chlorinated nickel, cobalt and iron are converted into gas at high temperature and enter the flue gas , in the recovery unit to wash, absorb and dissolve the chloride solution of the flue gas with water;

[0033] Co-precipitation conditions for a mixture of nickel-cobalt-iron compounds: add the above-mentioned chloride solution to the calcium hydroxide slurry, neutralize the precipitation temperature at 60°C, and react for 60 minutes. Recovery rate: nickel 90%, cob...

Embodiment 2

[0035] The nickel oxide ore composition used contains (weight%): Ni 1.65%, Fe 16.3%, Co 0.07%, MgO 15.8%, SiO 2 : 41.2%, CaO 0.2%, Al 2 o 3 5.28%, Cr 0.92%.

[0036] The nickel oxide ore and coke powder are crushed and ball milled respectively, and the fineness of the nickel oxide ore after ball milling is 100 mesh.

[0037] Chlorination roasting conditions: add 20% ammonium chloride, 0.5% coke powder and 5% sodium chloride according to the weight ratio of nickel oxide ore, roasting temperature 1210 ℃, roasting time 15 hours, make the nickel, cobalt and iron of chloride It is converted into gas at high temperature and enters the flue gas, and is washed with water in the recovery device to absorb and dissolve the chloride solution of the flue gas;

[0038] Co-precipitation conditions for a mixture of nickel-cobalt-iron compounds: add the above-mentioned chloride solution to the calcium hydroxide slurry, neutralize the precipitation temperature at 60°C, and react for 60 minut...

Embodiment 3

[0040] In the nickel oxide ore composition (weight %): Ni 1.82%, Fe 13.5%, CO 0.08%, MgO 16.5%, SiO 2 38.2%, CaO 0.32%, Al 2 o 3 4.57%, Cr 1.15%. The nickel oxide ore and coke powder are crushed and ball milled respectively, and the fineness of the nickel oxide ore after ball milling is 120 mesh.

[0041] Chlorination roasting conditions: add 30% sodium chloride and 0.5% coke powder according to the weight ratio of nickel oxide ore, roasting temperature 1220 ° C, roasting time 12 hours, so that the chlorinated nickel, cobalt and iron are converted into gas at high temperature and enter the smoke Gas, the chloride solution that washes, absorbs and dissolves the flue gas with water in the recovery unit;

[0042]Co-precipitation conditions for a mixture of nickel-cobalt-iron compounds: add the above-mentioned chloride solution to the calcium hydroxide slurry, neutralize the precipitation temperature at 70°C, and react for 75 minutes. Recovery rate: nickel 82%, cobalt 78%, iro...

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PUM

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Abstract

The invention relates to a technology for recovering nickel, cobalt and iron from nickel oxide ores through high-temperature chlorinating volatilization. The technology comprises the following steps: A, respectively pulverizing and ball-milling the nickel oxide ores and coke powder; B, uniformly mixing the nickel oxide ores, the coke powder and a chlorinating agent to carry out high-temperature chlorinating volatilization roasting, converting chlorinated nickel, cobalt and iron into gas at a high temperature, filling smoke, and in a recovering device, washing with water, absorbing and dissolving a smoke chloride solution; C, producing an oxyhydrogen mixture product containing nickel, cobalt and iron. The nickel grade of the oxyhydrogen mixture product containing nickel, cobalt and iron, produced by the invention, is high and can be used for producing stainless steel. Compared with the traditional nickel oxide ore wet-process treatment technology, the method for recovering nickel, cobalt and iron from nickel oxide ores belongs to the technology having the advantages of high resource comprehensive utilization rate, low energy consumption, environment friendliness and easiness for implementation.

Description

technical field [0001] The invention relates to hydrometallurgy, in particular to a process for recovering nickel-cobalt-iron by high-temperature chlorination and volatilization of nickel oxide ore. Background technique [0002] Nickel oxide ore is usually a symbiotic mineral containing a variety of metal elements. Contains iron, nickel, cobalt, manganese, aluminum and magnesium. In order to recycle these valuable metal elements, methods such as pyrometallurgy and hydrometallurgy have been adopted. [0003] The traditional pyrometallurgical treatment technologies of nickel oxide ore include rotary kiln drying pre-reduction-electric furnace reduction smelting to produce ferronickel; sintering-blast furnace sulfidation smelting to produce low matte nickel; and sintering-blast furnace reduction smelting to produce nickel pig iron. Rotary kiln drying pre-reduction-electric furnace reduction smelting is a classic process for processing nickel oxide ore. This method has the char...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B1/08C22B23/02
Inventor 毛黎生赵明会毛耐文
Owner 毛黎生
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