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Method for separating rare earth, iron, copper, cobalt and tungsten from alloy

A technology of alloys and rare earths, which is applied in the field of waste metal recycling, can solve problems such as pollution, operator influence, and high power consumption, and achieve the effects of simple process flow, low equipment requirements, and high recovery rate

Inactive Publication Date: 2008-05-28
PEKING UNIV FOUNDER GRP CO LTD +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of this type of method is: when the hard alloy is manually broken, it will cause pollution due to the metal material debris of the tool being brought into the broken material. In addition, because the hard alloy with a high cobalt content is not easy to break, the mechanical crushing method is limited Very limited; it is difficult to guarantee the quality of recycled products for cemented carbide mixtures with complex components;
The disadvantage of this type of method is: the power consumption in the whole process is relatively large, the high power consumption per ton of cemented carbide is about 12000KWh, and the low power consumption is more than 6000KWh; in addition, in the process of zinc melting and zinc collection, use Whether the equipment is reasonable will affect the recovery efficiency of zinc. Furthermore, the escape of zinc will have a certain impact on the operator

Method used

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  • Method for separating rare earth, iron, copper, cobalt and tungsten from alloy
  • Method for separating rare earth, iron, copper, cobalt and tungsten from alloy
  • Method for separating rare earth, iron, copper, cobalt and tungsten from alloy

Examples

Experimental program
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Effect test

Embodiment 1

[0086] 1 kg of NdFeB waste is separated and recycled. The main components of the waste metal are neodymium Nd and iron Fe, and contain a small amount of Co. The specific process of its treatment is as follows: after crushing the waste, put it in a container, add 500ml of water and stir, slowly add 6mol / L [H + ] 7L of sulfuric acid, 1Kg of 30wt% hydrogen peroxide, heated to 80°C to dissolve, and filtered to separate the solid and liquid. At this time, the solution contained RE ions, Fe ions and Co ions, heated the solution to 90°C, and added NaCl700g to generate a rare earth sulfate double salt precipitation. Add 4Kg of 30wt% liquid caustic soda to the filtered and washed precipitate, heat to 110°C for 4 hours, filter and wash, and dissolve in hydrochloric acid to obtain a rare earth chloride solution. The sulfate solution containing iron and cobalt is added with sodium carbonate to adjust the pH to 3 and precipitate to obtain ferric hydroxide to realize the separation and rec...

Embodiment 2

[0088] 1 kg of cemented carbide waste is separated and recycled. The main components of the cemented carbide waste are tungsten W, iron Fe, and cobalt Co. The specific process of its treatment is: after crushing the waste, put it in a container, slowly add 4L of 20wt% sulfuric acid, 500ml of 30wt% hydrogen peroxide, plug the container tightly, place it on a shaker and shake it at room temperature for 30 hours, and the tungsten carbide is suspended in the In the solution, tungsten can be recovered and utilized after centrifugal separation, washing and drying. The solution part is the sulfate of iron and cobalt. Sodium carbonate is added to adjust the pH to 2, and ferric hydroxide is precipitated, and iron is recovered through ferric hydroxide. Cobalt sulfate is precipitated and burned with oxalic acid to obtain cobalt oxide, and cobalt is recovered through cobalt oxide.

Embodiment 3

[0090] 1 kg of alloy waste from a cobalt salt factory, the main components are iron Fe, cobalt Co and copper Cu. After the alloy waste is broken, put it in an enamel reaction kettle, add water and stir, slowly add 6mol / L sulfuric acid, 30wt% hydrogen peroxide, keep the temperature at 90-95°C, and the reaction time is 12 hours. The concentration of the main chemical components in the leachate is For: Co45g / L, Cu20g / L, Fe30g / L. Heating the leaching solution to 85°C, adding 20wt% sodium carbonate solution for neutralization, controlling the pH value in the range of 3.2-3.4, when the Fe in the feed solution is less than 0.5g / L, filter and wash the iron hydroxide precipitate, and remove it from hydrogen Iron recovery from iron oxide precipitation. After removing iron, heat the feed liquid to 80°C, add 20wt% sodium carbonate solution, adjust the pH value of the feed liquid to 4.2-4.4, form and precipitate copper hydroxide, and the feed liquid is mainly cobalt, which can be used to ...

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Abstract

The invention discloses a process for separating rare earth, copper, iron, cobalt, and tungsten from alloys. The treating process of the separation of the rare earth is that sulphuric acid and hydrogen dioxide solution are added to the alloy, the alloy is quickly dissolved to sulphate solution, and alkali metal salt or alkaline earth metal salt is added to the sulphate solution to generate sulfuric double salt precipitation of the rare earth, the sulfuric double salt precipitation is added with alkali and is converted to rare earth hydrate, and the rare earth hydrate is treated and rare earth is recycled. The treating process of the separation of copper, iron, cobalt, and tungsten is that sulphuric acid and hydrogen dioxide solution are added to the alloy, the alloy is quickly dissolved to sulphate solution, and the precipitation of tungsten carbide is simultaneously separated out, alkali is added to the sulphate solution after the solid-liquid separation, the precipitations corresponding to iron, copper and cobalt are respectively separated out by adjusting pH values of different ranges, and copper, iron, cobalt, and tungsten are recycled through the separated precipitations. The invention has low level of facility request, and the whole technology process is simpler, cleaner and safer, and the recovery ratio is high and the energy consumption is low.

Description

technical field [0001] The invention relates to the field of waste metal regeneration treatment, in particular to a method for separating rare earth, iron, copper, cobalt and tungsten from alloys. Background technique [0002] With the improvement of the production and consumption level of non-ferrous metals in our country, the accumulation of waste and miscellaneous metals available in the society is also increasing, including waste rocks, waste residues, waste liquids, waste gases and Useful mineral components in tailings, as well as scrap metals, etc. The extraction and utilization of useful components in these industrial wastes and the reuse of waste industrial products can not only improve the utilization rate of non-ferrous metal resources, but also reduce pollution, protect the ecological environment, save precious metal resources, and play a role in the creation of social civilization and progress. to a positive effect. In addition, mineral resources are non-renewa...

Claims

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Application Information

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IPC IPC(8): C22B3/08C22B3/46C22B3/26C22B3/22C22B59/00C21B15/00C22B15/00C22B23/00C22B34/36
CPCY02P10/20
Inventor 王嵩龄贾江涛严纯华
Owner PEKING UNIV FOUNDER GRP CO LTD
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