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Method for double-flash direct comprehensive recovery of neodymium iron boron waste

A neodymium iron boron and waste technology is applied in the field of direct and comprehensive recovery of neodymium iron boron waste double flash, which can solve the problems of inability to precisely control temperature and atmosphere, decrease in the total recovery rate of rare earth, and difficult comprehensive utilization of leaching slag, and achieve superior reaction power. Learning conditions, furnace atmosphere is easy to control, and the effect of good popularization and application value

Active Publication Date: 2019-03-22
JIANGXI UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The first stage of rotary kiln roasting is mainly to remove the oil in the NdFeB sludge and provide raw materials for the second stage of deep oxidation. However, due to the inherent defects of the rotary kiln, the temperature and atmosphere cannot be precisely controlled, and the deoiling process is often insufficiently burned, resulting in High energy consumption, and often black smoke, polluting the environment
The second stage of rotary kiln roasting often oxidizes rare earth and iron into RE as much as possible. 2 o 3 and Fe 2 o 3 , due to the slow oxidation reaction rate of the rotary kiln, it often takes 4-8 hours to achieve a high oxidation rate, and, due to the use of two-stage rotary kiln, the volume is large, the area is large, the external heat dissipation area is large, and there is heat-cold alternation link, high energy consumption
In addition, since the rare earth and iron are leached with hydrochloric acid after the simultaneous oxidation of rare earth and iron, a large amount of iron in the waste enters the acid leaching slag, the amount of slag is large, and the total amount of rare earth taken away by the slag is large, resulting in a decrease in the total recovery rate of rare earth, while the leaching slag It is difficult to get a good comprehensive utilization by itself, and it is often stockpiled, causing environmental pollution

Method used

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  • Method for double-flash direct comprehensive recovery of neodymium iron boron waste
  • Method for double-flash direct comprehensive recovery of neodymium iron boron waste
  • Method for double-flash direct comprehensive recovery of neodymium iron boron waste

Examples

Experimental program
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Effect test

Embodiment 1

[0028] Spray the powdery NdFeB waste with a particle size of 100 mesh and oxygen-enriched air with an oxygen mass percentage concentration of 40% into a reaction tower (2) with a height of 2.5 meters and a temperature of 800 °C through a nozzle (1). In a highly dispersed floating state, it falls from the upper end of the reaction tower to the lower end. During this process, the iron and rare earth in the material are rapidly oxidized by oxygen-enriched air. The oxidation rate of iron in the waste is 99.41%, and the oxidation rate of rare earth is 99.82%. Oxidation products fall into the collector (3) below the reaction tower, and are released from the outlet (4) before entering the flash reduction furnace. The oxidized flue gas is discharged through the flue (5) at the upper end of the collector (3), and is emptied after dust collection.

[0029] After the flash oxidation product is mixed with 6% CaO powder by weight of the product, it is sprayed together with hydrogen into a ...

Embodiment 2

[0031] Spray the powdery NdFeB waste with a particle size of 200 mesh and oxygen-enriched air with an oxygen mass percentage concentration of 30% into a reaction tower (2) with a height of 3.5 meters and a temperature of 1000 °C through a nozzle (1). In a highly dispersed floating state, it falls from the upper end of the reaction tower to the lower end. During this process, the iron and rare earth in the material are rapidly oxidized by oxygen-enriched air. The oxidation rate of iron in the waste is 99.85%, and the oxidation rate of rare earth is 99.94%. Oxidation products fall into the collector (3) below the reaction tower, and are released from the outlet (4) before entering the flash reduction furnace. The oxidized flue gas is discharged through the flue (5) at the upper end of the collector (3), and is emptied after dust collection.

[0032] The flash oxidation product was mixed with 5% SiO by weight of the product 2 After the powder is mixed, it is sprayed together wit...

Embodiment 3

[0034] Spray the powdery NdFeB waste with a particle size of 300 mesh and oxygen-enriched air with an oxygen mass percentage concentration of 50% into a reaction tower (2) with a height of 2.5 meters and a temperature of 900 °C through a nozzle (1). In a highly dispersed floating state, it falls from the upper end of the reaction tower to the lower end. During this process, the iron and rare earth in the material are rapidly oxidized by the oxygen-enriched air. The oxidation rate of iron in the waste is 99.75%, and the oxidation rate of rare earth is 99.91%. Oxidation products fall into the collector (3) below the reaction tower, and are released from the outlet (4) before entering the flash reduction furnace. The oxidized flue gas is discharged through the flue (5) at the upper end of the collector (3), and is emptied after dust collection.

[0035] The flash oxidation product was mixed with 3% SiO by weight of the product 2Powder and 2% CaO powder are mixed, sprayed togethe...

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Abstract

The invention discloses a method for double-flash direct comprehensive recovery of neodymium iron boron waste. The method comprises the steps that the neodymium iron boron waste and oxygen-rich air are sprayed into a high-temperature vertical reaction tower together through a nozzle, materials float down from the upper end of the reaction tower to the lower end of the reaction tower in a highly dispersed floating state, and rare earth and iron in the materials are quickly and fully oxidized; oxidation products and reductive gas are sprayed into another high-temperature vertical reaction towertogether through a nozzle, iron oxide in the materials is mostly reduced into metal iron, and when passing through a hot coke layer on a settling pond, a small amount of non-reduced iron is reduced into metal iron; and after standing layering, molten iron and rare earth slag are discharged out from an iron outlet and a slag discharging outlet. According to the method, efficient enrichment and separation of the rare earth and the iron in the neodymium iron boron waste are realized, the defects that by adopting a traditional neodymium iron boron waste treatment method, the process is long, energy consumption is high, the rare earth and the iron cannot be separated before acid dissolution, the acid dissolution iron slag amount is large, the rare earth recovery rate is low, and iron resourcesare difficult to recover are overcome, and good economic and environmental protection benefits are achieved.

Description

technical field [0001] The invention relates to a method for direct and comprehensive recovery of NdFeB waste double flash, belonging to the technical field of rare earth metallurgy. Background technique [0002] NdFeB is a magnetic material. As the latest achievement in the development of rare earth permanent magnet materials, it is known as the "Magnetic King" because of its excellent magnetic properties and is widely used in various fields. In the production process of NdFeB magnetic materials, about 20-25% of waste will be generated, most of which are NdFeB sludge waste. These scraps contain about 60% iron and about 30% rare earth elements. The recycling of NdFeB waste not only rationally utilizes resources, but also reduces environmental pollution. [0003] At present, NdFeB oil sludge waste is often roasted in a two-stage rotary kiln, and then leached-extracted-precipitated-burned to recover the rare earths. The first stage of rotary kiln roasting is mainly to remov...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B59/00C22B1/00
CPCC22B1/005C22B7/007C22B59/00Y02P10/20
Inventor 汪金良刘付朋陈早明
Owner JIANGXI UNIV OF SCI & TECH
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