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CN117187600A - A method for recovering all rare earth elements from rare earth magnetic material waste - Google Patents

A method for recovering all rare earth elements from rare earth magnetic material waste Download PDF

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CN117187600A
CN117187600A CN202311211329.8A CN202311211329A CN117187600A CN 117187600 A CN117187600 A CN 117187600A CN 202311211329 A CN202311211329 A CN 202311211329A CN 117187600 A CN117187600 A CN 117187600A
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rare earth
oxide
carbon
waste
magnetic material
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王德盛
张永健
崔红岩
韩小亮
胡华兵
魏金海
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Fujian Changting Jinlong Rare Earth Co Ltd
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Fujian Changting Jinlong Rare Earth Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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Abstract

The invention provides a method for recycling all rare earth elements in rare earth magnetic material waste, which comprises the following steps of firstly crushing, burning and oxidizing the rare earth magnetic material waste to obtain sufficient oxide; and then mixing the sufficient oxide obtained in the steps with carbon, reducing the mixture through heat treatment, cooling the mixture, and separating the mixture to obtain the metal material and the rare earth oxide. The invention firstly carries out impurity removal, crushing and oxidation treatment on materials, converts rare earth metals, iron and other metals into oxides, reduces the iron, copper and other oxides into metals through a carbon reduction body, ensures that the metals are in a liquid state, ensures that the oxides are in a solid state, and is poured into a mold, and after cooling, the metals and the oxides are effectively separated through a physical method. The invention can realize the full recycling of metals in the rare earth magnetic material waste, has simple and convenient operation, continuous and controllable process, low cost, no need of acid and alkali, no waste water, no toxic gas discharge and no waste, and is suitable for continuous operation.

Description

一种稀土磁性材料废料中全稀土元素回收方法A method for recovering all rare earth elements from rare earth magnetic material waste

技术领域Technical field

本发明属于稀土磁性材料废料回收技术领域,涉及一种稀土磁性材料废料中全稀土元素回收方法。The invention belongs to the technical field of rare earth magnetic material waste recycling and relates to a method for recovering all rare earth elements in rare earth magnetic material waste.

背景技术Background technique

钕铁硼永磁材料因其优越的磁性性能,现已广泛应用于国防军工、航空航天、医疗器械、计算机、电子、机器人和新能源汽车工业等领域。NdFeB permanent magnet materials have been widely used in defense industry, aerospace, medical equipment, computers, electronics, robots and new energy automobile industries due to their superior magnetic properties.

现今全球每年生产的R-Fe-B系永磁体在三十万吨以上,制造工序中将产生磁铁碎屑、切削屑、碾磨屑、超细粉等废料占投入物料比例的25~35%。而且随着时间的推移,作为各产品部件的永磁体也会逐渐到期报废,如电力机械、医疗器械、玩具、包装、五金机械、航天航空等领域较常见的利用R-Fe-B系永磁体有永磁电机、扬声器、磁选机、计算机磁盘驱动器、磁共振成像设备仪表等。现有技术中也公开了类似的回收处理的技术方案,如CN97120123.4中公开了稀土类化合物的回收方法,一种稀土类化合物的回收方法,包括如下步骤:(1)回收原料的初步处理;(2)稀土类化合物的酸溶液浸出;(3)过滤;(4)含稀土类金属离子溶液的沉淀析出;(5)沉淀物烘干、灼烧。但是,该技术方案所用的方法中,两次以上需要使用酸,需要使用干净的水清洗,而且需要两次以上的烘干、焙烧,需要消耗大量的酸,产生酸性溶液需要处理,需要消耗大量的水和能源,不仅工艺流程长,而且稀土收率不高。同时,磁性废料中所含的大量铁被以盐溶液的形式排放,或以其它固态废料形式堆放。少量的其它金属如铜、铝、钴、铌等也被以废弃物处理,未能得到回收利用。再如,CN201580016947.4也公开了稀土元素的回收方法,具体公开了:对于至少含有稀土元素与铁族元素的处理对象物进行了氧化处理之后,通过将处理环境转移至碳的存在下进行热处理,从而将稀土元素作为氧化物从铁族元素中分离并回收的方法。但该方法也存在以下缺陷,①由于采用真空或非活性气氛,设备结构复杂价格昂贵,有气体放出的反应抽真空,真空度难以达到目标值,运行时间将较长。②碳与氧化物物料分层放置,造成碳与铁的氧化物接触不好,计算与实践证明碳与氧化铁或四氧化三铁的反应生成产物均主要为一氧化碳--属于固固反应,接触不好将严重影响反应速度和程度,有可能造成铁的氧化物含量过高。③资源未能得到充分利用,铁族金属及其它少量金属的利用未实现。④操作便利性较差。Today, more than 300,000 tons of R-Fe-B series permanent magnets are produced globally every year. Waste materials such as magnet chips, cutting chips, grinding chips, and ultrafine powder will be generated during the manufacturing process, accounting for 25 to 35% of the input materials. . And as time goes by, permanent magnets as components of various products will gradually expire and be scrapped, such as the more common R-Fe-B series permanent magnets in electric machinery, medical equipment, toys, packaging, hardware machinery, aerospace and other fields. Magnets include permanent magnet motors, speakers, magnetic separators, computer disk drives, magnetic resonance imaging equipment instruments, etc. Similar technical solutions for recycling are also disclosed in the prior art. For example, CN97120123.4 discloses a method for recycling rare earth compounds. A method for recycling rare earth compounds includes the following steps: (1) Preliminary treatment of recycled raw materials ; (2) Leaching of acid solutions of rare earth compounds; (3) Filtration; (4) Precipitation of solutions containing rare earth metal ions; (5) Drying and burning of precipitates. However, in the method used in this technical solution, acid needs to be used more than twice, clean water needs to be used, and drying and roasting need to be done more than twice, which requires a large amount of acid consumption, and the acidic solution needs to be processed, which requires a large amount of consumption. Not only does the process require a long process, but the rare earth yield is not high. At the same time, large amounts of iron contained in magnetic waste are discharged as salt solutions or piled up as other solid waste. Small amounts of other metals such as copper, aluminum, cobalt, niobium, etc. are also treated as waste and cannot be recycled. For another example, CN201580016947.4 also discloses a method for recovering rare earth elements. Specifically, it discloses that after oxidizing treatment objects containing at least rare earth elements and iron group elements, the treatment environment is transferred to the presence of carbon for heat treatment. , thereby separating and recovering rare earth elements as oxides from iron group elements. However, this method also has the following shortcomings: ① Due to the use of vacuum or inactive atmosphere, the equipment structure is complex and expensive, and the reaction with gas release is evacuated, and the vacuum degree is difficult to reach the target value, and the running time will be long. ② Carbon and oxide materials are placed in layers, resulting in poor contact between carbon and iron oxides. Calculations and practice have proven that the reaction products between carbon and iron oxide or ferric oxide are mainly carbon monoxide - a solid-solid reaction, contact Failure to do so will seriously affect the reaction speed and extent, and may cause the iron oxide content to be too high. ③Resources have not been fully utilized, and the utilization of iron group metals and other small amounts of metals has not been realized. ④The operation convenience is poor.

因此,如何提供一种更为适宜的方法,能够将其中所含的各种元素特别是稀土元素进行低成本、绿色回收成为当下重要的技术课题,也是业内诸多一线研究人员亟待解决的问题之一。Therefore, how to provide a more appropriate method for low-cost and green recycling of various elements, especially rare earth elements, has become an important technical issue at the moment, and it is also one of the issues that many front-line researchers in the industry urgently need to solve. .

发明内容Contents of the invention

有鉴于此,本发明要解决的技术问题在于提供一种稀土磁性材料废料中全稀土元素回收方法。这是一种充分利用稀土磁性材料废料中的金属,实现全部回收利用稀土磁性材料中的金属的处理稀土磁性材料废料的方法,本发明可以从稀土磁性材料废料回收稀土氧化物及其它金属,该方法操作简单,低成本、无酸碱连续循环、无废弃物、适合连续作业,更加适于规模化工业生产的推广和应用。In view of this, the technical problem to be solved by the present invention is to provide a method for recovering all rare earth elements in rare earth magnetic material waste. This is a method for processing rare earth magnetic material waste that fully utilizes the metal in the rare earth magnetic material waste and realizes the full recycling of the metal in the rare earth magnetic material. The present invention can recover rare earth oxides and other metals from the rare earth magnetic material waste. The method has simple operation, low cost, no acid-base continuous cycle, no waste, is suitable for continuous operation, and is more suitable for the promotion and application of large-scale industrial production.

本发明提供了一种稀土磁性材料废料中全稀土元素回收方法,包括以下步骤:The invention provides a method for recovering all rare earth elements in rare earth magnetic material waste, which includes the following steps:

1)将稀土磁性材料废料进行粉碎和燃烧氧化后,得到充分氧化物;1) After crushing, burning and oxidizing the rare earth magnetic material waste, sufficient oxides are obtained;

2)将上述步骤得到的充分氧化物与碳混合,经过热处理还原后,然后进行冷却,分离后得到金属物料和稀土氧化物。2) Mix the sufficient oxides obtained in the above steps with carbon, reduce them through heat treatment, then cool them, and then separate them to obtain metal materials and rare earth oxides.

优选的,所述粉碎后的稀土磁性材料废料的粒度小于等于0.061mm;Preferably, the particle size of the crushed rare earth magnetic material waste is less than or equal to 0.061mm;

所述燃烧氧化的方式在含氧气氛下进行燃烧氧化;The combustion oxidation method carries out combustion oxidation in an oxygen-containing atmosphere;

所述含氧气氛的氧气体积含量为4%~21%。The oxygen volume content of the oxygen-containing atmosphere is 4% to 21%.

优选的,所述燃烧氧化的温度为大于等于500℃;Preferably, the temperature of the combustion oxidation is greater than or equal to 500°C;

所述燃烧氧化的时间为12~24h。The combustion and oxidation time is 12 to 24 hours.

优选的,所述稀土磁性材料废料中包含镧、铈、镨、钕、钐、铕、钆、铽、镝、钬、铒、铥、镱、镥、钪和钇中的一种或多种稀土元素;Preferably, the rare earth magnetic material waste contains one or more rare earths selected from the group consisting of lanthanum, cerium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, scandium and yttrium. element;

所述充分氧化物与碳的质量比为,以充分氧化物中的Fe元素计,Fe与碳的质量比为(2.4~2.8):1;The mass ratio of the sufficient oxide to carbon is, based on the Fe element in the sufficient oxide, the mass ratio of Fe to carbon is (2.4-2.8): 1;

所述碳包括高炉焦、沥青焦和木炭中的一种或多种。The carbon includes one or more of blast furnace coke, pitch coke and charcoal.

优选的,所述碳包括稀土熔盐电解废阳极和/或废石墨槽;Preferably, the carbon includes waste rare earth molten salt electrolysis anodes and/or waste graphite tanks;

所述热处理还原的温度为大于等于710℃;The temperature of the heat treatment reduction is greater than or equal to 710°C;

所述热处理还原的时间为4~6h。The heat treatment reduction time is 4 to 6 hours.

优选的,所述分离的方式包括剥离;Preferably, the separation method includes peeling;

所述冷却后,得到的物料中,稀土氧化物位于物料上层;After the cooling, in the obtained material, the rare earth oxide is located in the upper layer of the material;

所述稀土氧化物具有松散的团状结构。The rare earth oxide has a loose mass structure.

优选的,所述稀土氧化物中还包括碳、铝氧化物、钛氧化物、铌氧化物和铁氧化物中的一种或多种;Preferably, the rare earth oxide also includes one or more of carbon, aluminum oxide, titanium oxide, niobium oxide and iron oxide;

所述铝氧化物在稀土氧化物中的质量含量为0.1%~0.5%。The mass content of the aluminum oxide in the rare earth oxide is 0.1% to 0.5%.

优选的,所述钛氧化物在稀土氧化物中的质量含量为0.03%~0.10%;Preferably, the mass content of the titanium oxide in the rare earth oxide is 0.03% to 0.10%;

所述铌氧化物在稀土氧化物中的质量含量为0.03%~0.3%;The mass content of the niobium oxide in the rare earth oxide is 0.03% to 0.3%;

所述铁氧化物在稀土氧化物中的质量含量为0.3%~10%。The mass content of the iron oxide in the rare earth oxide is 0.3% to 10%.

优选的,所述金属物料包括铁族元素合金;Preferably, the metal material includes an alloy of iron group elements;

所述金属物料还包括稀土元素、铝元素和碳元素中的一种或多种。The metal material also includes one or more of rare earth elements, aluminum elements and carbon elements.

优选的,所述稀土元素在金属物料中的质量含量为90%~99.5%;Preferably, the mass content of the rare earth elements in the metal material is 90% to 99.5%;

所述铝元素在金属物料中的质量含量为0.03%~0.10%;The mass content of the aluminum element in the metal material is 0.03% to 0.10%;

所述碳元素在金属物料中的质量含量为0.005%~0.1%。The mass content of the carbon element in the metal material is 0.005% to 0.1%.

本发明提供了一种稀土磁性材料废料中全稀土元素回收方法,包括以下步骤,首先将稀土磁性材料废料进行粉碎和燃烧氧化后,得到充分氧化物;然后将上述步骤得到的充分氧化物与碳混合,经过热处理还原后,然后进行冷却,分离后得到金属物料和稀土氧化物。与现有技术相比,本发明创造性的设计了一种具有特定工艺路线和工艺参数的回收方法,这是一种充分利用稀土磁性材料废料中的金属,实现全部回收利用稀土磁性材料中的金属的处理稀土磁性材料废料的方法。本发明可以从稀土磁性材料废料回收稀土氧化物及其它金属,该方法操作简单,低成本、无酸碱连续循环、无废弃物、适合连续作业。The invention provides a method for recovering all rare earth elements in rare earth magnetic material waste, which includes the following steps: first, the rare earth magnetic material waste is crushed, burned and oxidized to obtain sufficient oxides; and then the sufficient oxides obtained in the above steps are mixed with carbon After mixing, reduction through heat treatment, cooling, and separation, metal materials and rare earth oxides are obtained. Compared with the existing technology, the present invention creatively designs a recycling method with specific process routes and process parameters. This method fully utilizes the metal in the rare earth magnetic material waste and realizes the full recycling of the metal in the rare earth magnetic material. Methods for processing rare earth magnetic material waste. The invention can recover rare earth oxides and other metals from rare earth magnetic material waste. The method has simple operation, low cost, no acid and alkali continuous circulation, no waste, and is suitable for continuous operation.

本发明通过先对物料进行除杂、粉碎、氧化处理,将稀土金属及铁等金属转为氧化物,通过碳还原体将铁、铜等的氧化物还原为金属,金属处于液态,氧化物处于固态,浇注入模具,冷却后通过物理方法将金属与氧化物进行有效分离。本发明通过该回收工艺可实现对稀土磁性材料废料中金属的全回收利用,而且操作简单方便,工艺连续可控,低成本、不需要使用酸碱,不产生废水,不排放有毒气体,无废弃物,对环境污染极少,适合连续作业,更加适于规模化工业生产的推广和应用。This invention first removes impurities, crushes and oxidizes the materials, converts rare earth metals, iron and other metals into oxides, and reduces the oxides of iron, copper, etc. into metals through carbon reducers. The metals are in a liquid state and the oxides are in a liquid state. In solid state, it is poured into a mold, and after cooling, the metal and oxide are effectively separated by physical methods. The present invention can realize full recycling of metals in rare earth magnetic material waste through this recycling process, and the operation is simple and convenient, the process is continuously controllable, low cost, does not require the use of acids and bases, does not produce waste water, does not emit toxic gases, and has no waste. It has very little environmental pollution, is suitable for continuous operation, and is more suitable for the promotion and application of large-scale industrial production.

实验结果表明,采用本发明提供的从稀土材料废料中全稀土元素回收方法,收率大于92.5%,大于行业的90%,而且回收路径简单,无废弃物产生,成本低。Experimental results show that using the method for recovering all rare earth elements from rare earth material waste provided by the present invention, the yield is greater than 92.5%, which is greater than 90% of the industry, and the recovery path is simple, no waste is generated, and the cost is low.

具体实施方式Detailed ways

为了进一步理解本发明,下面结合实施例对本发明优选实施方案进行描述,但是应当理解,这些描述只是为了进一步说明本发明的特征和优点,而不是对发明权利要求的限制。In order to further understand the present invention, the preferred embodiments of the present invention are described below in conjunction with the examples. However, it should be understood that these descriptions are only to further illustrate the features and advantages of the present invention and are not intended to limit the claims of the invention.

本发明所有原料,对其来源没有特别限制,在市场上购买的或按照本领域技术人员熟知的常规方法制备的即可。All raw materials of the present invention have no particular restrictions on their sources. They can be purchased in the market or prepared according to conventional methods well known to those skilled in the art.

本发明所有原料,对其纯度没有特别限制,本发明优选采用工业纯或钕铁硼磁体回收再利用领域使用的常规纯度。There is no particular limit on the purity of all the raw materials in the present invention. The present invention preferably adopts industrial purity or conventional purity used in the field of NdFeB magnet recycling.

本发明提供了一种稀土磁性材料废料中全稀土元素回收方法,包括以下步骤:The invention provides a method for recovering all rare earth elements in rare earth magnetic material waste, which includes the following steps:

1)将稀土磁性材料废料进行粉碎和燃烧氧化后,得到充分氧化物;1) After crushing, burning and oxidizing the rare earth magnetic material waste, sufficient oxides are obtained;

2)将上述步骤得到的充分氧化物与碳混合,经过热处理还原后,然后进行冷却,分离后得到金属物料和稀土氧化物。2) Mix the sufficient oxides obtained in the above steps with carbon, reduce them through heat treatment, then cool them, and then separate them to obtain metal materials and rare earth oxides.

在本发明中,全稀土元素优选是指对稀土磁性材料废料中的稀土种类的元素均进行回收,包括轻稀土和/或重稀土。该回收方法属于火法回收方法。In the present invention, all rare earth elements preferably refer to the recovery of all rare earth elements in the rare earth magnetic material waste, including light rare earths and/or heavy rare earths. This recycling method belongs to the fire recycling method.

本发明首先将稀土磁性材料废料进行粉碎和燃烧氧化后,得到充分氧化物。In the present invention, the rare earth magnetic material waste is first crushed, burned and oxidized to obtain sufficient oxides.

在本发明中,所述粉碎后的稀土磁性材料废料的粒度优选小于等于0.061mm,更优选小于等于0.06mm,小于等于0.059mm。In the present invention, the particle size of the pulverized rare earth magnetic material waste is preferably less than or equal to 0.061 mm, more preferably less than or equal to 0.06 mm, and less than or equal to 0.059 mm.

在本发明中,所述燃烧氧化的方式优选在含氧气氛下进行燃烧氧化。In the present invention, the combustion oxidation method is preferably carried out in an oxygen-containing atmosphere.

在本发明中,所述含氧气氛的氧气体积含量优选为4%~21%,更优选为8%~17%,更优选为11%~13%。In the present invention, the oxygen volume content of the oxygen-containing atmosphere is preferably 4% to 21%, more preferably 8% to 17%, and more preferably 11% to 13%.

在本发明中,所述燃烧氧化的温度优选为大于等于500℃,更优选大于等于600℃,更优选大于等于800℃。具体可以为500~1450℃,或者为600~1350℃,或者为700~1250℃,或者为800~1150℃。In the present invention, the temperature of the combustion oxidation is preferably greater than or equal to 500°C, more preferably greater than or equal to 600°C, and even more preferably greater than or equal to 800°C. Specifically, it can be 500-1450°C, or 600-1350°C, or 700-1250°C, or 800-1150°C.

在本发明中,所述燃烧氧化的时间优选为12~24h,更优选为14~22h,更优选为16~20h。In the present invention, the combustion and oxidation time is preferably 12 to 24 hours, more preferably 14 to 22 hours, and more preferably 16 to 20 hours.

在本发明中,所述稀土磁性材料废料中优选包含镧、铈、镨、钕、钐、铕、钆、铽、镝、钬、铒、铥、镱、镥、钪和钇中的一种或多种稀土元素,更优选为镧、铈、镨、钕、钐、铕、钆、铽、镝、钬、铒、铥、镱、镥、钪和钇中的一种稀土元素。In the present invention, the rare earth magnetic material waste preferably contains one of lanthanum, cerium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, scandium and yttrium or A variety of rare earth elements are more preferably one of lanthanum, cerium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, scandium and yttrium.

本发明最后将上述步骤得到的充分氧化物与碳混合,经过热处理还原后,然后进行冷却,分离后得到金属物料和稀土氧化物。Finally, in the present invention, the sufficient oxide obtained in the above steps is mixed with carbon, reduced through heat treatment, then cooled, and separated to obtain metal materials and rare earth oxides.

在本发明中,所述充分氧化物与碳的质量比为,以充分氧化物中的Fe元素计,Fe与碳的质量比优选为(2.4~2.8):1,更优选为(2.45~2.75):1,更优选为(2.5~2.7):1,更优选为(2.55~2.65):1。In the present invention, the mass ratio of the sufficient oxide to carbon is, based on the Fe element in the sufficient oxide, the mass ratio of Fe to carbon is preferably (2.4-2.8):1, more preferably (2.45-2.75 ): 1, more preferably (2.5-2.7): 1, more preferably (2.55-2.65): 1.

在本发明中,所述碳优选包括高炉焦、沥青焦和木炭中的一种或多种,更优选为高炉焦、沥青焦或木炭。In the present invention, the carbon preferably includes one or more of blast furnace coke, pitch coke and charcoal, more preferably blast furnace coke, pitch coke or charcoal.

在本发明中,所述碳优选包括稀土熔盐电解废阳极和/或废石墨槽,更优选为稀土熔盐电解废阳极或废石墨槽。In the present invention, the carbon preferably includes waste rare earth molten salt electrolysis anodes and/or waste graphite tanks, and more preferably is waste rare earth molten salt electrolysis anodes or waste graphite tanks.

在本发明中,所述热处理还原的温度优选为大于等于710℃,更优选为大于等于750℃,大于等于800℃。具体可以为710~1450℃,或者为800~1200℃,或者为900~1100℃。In the present invention, the temperature of the heat treatment reduction is preferably equal to or greater than 710°C, more preferably equal to or greater than 750°C, and greater than or equal to 800°C. Specifically, it can be 710-1450°C, or 800-1200°C, or 900-1100°C.

在本发明中,所述热处理还原的时间优选为4~6h,更优选为4.4~5.6h,更优选为4.8~5.2h。In the present invention, the heat treatment reduction time is preferably 4 to 6 hours, more preferably 4.4 to 5.6 hours, and more preferably 4.8 to 5.2 hours.

在本发明中,所述分离的方式优选包括剥离。In the present invention, the separation method preferably includes peeling off.

在本发明中,所述冷却后,得到的物料中,稀土氧化物优选位于物料上层。In the present invention, in the material obtained after the cooling, the rare earth oxide is preferably located in the upper layer of the material.

在本发明中,所述稀土氧化物优选具有松散的团状结构。In the present invention, the rare earth oxide preferably has a loose mass structure.

在本发明中,所述稀土氧化物中还优选包括碳、铝氧化物、钛氧化物、铌氧化物和铁氧化物中的一种或多种,更优选为碳、铝氧化物、钛氧化物、铌氧化物或铁氧化物。具体的,所述铁氧化物优选包括二氧化三铁和四氧化三铁,其中,二氧化三铁≤10%,四氧化三铁>90%。In the present invention, the rare earth oxide preferably includes one or more of carbon, aluminum oxide, titanium oxide, niobium oxide and iron oxide, and more preferably carbon, aluminum oxide, titanium oxide substance, niobium oxide or iron oxide. Specifically, the iron oxide preferably includes ferric oxide and ferric tetroxide, wherein ferric oxide is ≤10% and ferric oxide is >90%.

在本发明中,所述铝氧化物在稀土氧化物中的质量含量优选为0.1%~0.5%,更优选为0.15%~0.45%,更优选为0.2%~0.4%,更优选为0.25%~0.35%。In the present invention, the mass content of the aluminum oxide in the rare earth oxide is preferably 0.1% to 0.5%, more preferably 0.15% to 0.45%, more preferably 0.2% to 0.4%, and more preferably 0.25% to 0.25%. 0.35%.

在本发明中,所述钛氧化物在稀土氧化物中的质量含量优选为0.03%~0.10%,更优选为0.04%~0.09%,更优选为0.05%~0.08%,更优选为0.06%~0.07%。In the present invention, the mass content of the titanium oxide in the rare earth oxide is preferably 0.03% to 0.10%, more preferably 0.04% to 0.09%, more preferably 0.05% to 0.08%, and more preferably 0.06% to 0.06%. 0.07%.

在本发明中,所述铌氧化物在稀土氧化物中的质量含量优选为0.03%~0.3%,更优选为0.08%~0.25%,更优选为0.13%~0.2%。In the present invention, the mass content of the niobium oxide in the rare earth oxide is preferably 0.03% to 0.3%, more preferably 0.08% to 0.25%, and more preferably 0.13% to 0.2%.

在本发明中,所述铁氧化物在稀土氧化物中的质量含量优选为0.3%~10%,更优选为2%~8%,更优选为4%~6%。In the present invention, the mass content of the iron oxide in the rare earth oxide is preferably 0.3% to 10%, more preferably 2% to 8%, and more preferably 4% to 6%.

在本发明中,所述金属物料优选包括铁族元素合金。In the present invention, the metal material preferably includes an iron group element alloy.

在本发明中,所述金属物料还优选包括稀土元素、铝元素和碳元素中的一种或多种,更优选为稀土元素、铝元素或碳元素。In the present invention, the metal material preferably includes one or more of rare earth elements, aluminum elements and carbon elements, more preferably rare earth elements, aluminum elements or carbon elements.

在本发明中,所述稀土元素在金属物料中的质量含量优选为90%~99.5%,更优选为92%~98%,更优选为94%~96%。In the present invention, the mass content of the rare earth element in the metal material is preferably 90% to 99.5%, more preferably 92% to 98%, and more preferably 94% to 96%.

在本发明中,所述铝元素在金属物料中的质量含量优选为0.03%~0.10%,更优选为0.04%~0.09%,更优选为0.05%~0.08%,更优选为0.06%~0.07%。In the present invention, the mass content of the aluminum element in the metal material is preferably 0.03% to 0.10%, more preferably 0.04% to 0.09%, more preferably 0.05% to 0.08%, and more preferably 0.06% to 0.07% .

在本发明中,所述碳元素在金属物料中的质量含量优选为0.005%~0.1%,更优选为0.01%~0.08%,更优选为0.03%~0.06%。In the present invention, the mass content of the carbon element in the metal material is preferably 0.005% to 0.1%, more preferably 0.01% to 0.08%, and more preferably 0.03% to 0.06%.

本发明为完整和细化整体技术方案,更好的提高回收效率和工艺连续性,降低回收成本和环境影响,上述稀土磁性材料废料中全稀土元素回收方法具体可以为以下步骤:The present invention is a complete and refined overall technical solution, which can better improve recycling efficiency and process continuity, reduce recycling costs and environmental impact. The above-mentioned recovery method of all rare earth elements in rare earth magnetic material waste can specifically include the following steps:

一种稀土磁性材料废料中全稀土元素回收方法,包括如下步骤:A method for recovering all rare earth elements in rare earth magnetic material waste, including the following steps:

步骤(1):将粉碎后物料加入回转窑进行充分氧化;Step (1): Add the crushed material to the rotary kiln for full oxidation;

步骤(2):将充分氧化物的物料与适量的碳粉进行混合均匀,放入至加热装置中;Step (2): Mix the fully oxidized material and an appropriate amount of carbon powder evenly, and put it into the heating device;

步骤(3):对加热装置进行升温,碳颗粒与铁族元素的氧化物进行充分地还原反应,铁族元素的氧化物被还原为铁族金属;Step (3): The heating device is heated, the carbon particles and the oxides of the iron group elements are fully reduced, and the oxides of the iron group elements are reduced to iron group metals;

步骤(4):将步骤(3)反应后的物料倒入模具中,模具采用水冷进行冷却。冷却至100℃以下;Step (4): Pour the material reacted in step (3) into the mold, and the mold is cooled by water cooling. Cool to below 100℃;

步骤(5):对步骤(4)中的冷却后的物料进行分离,得到稀土氧化物,微量的铝氧化物、钛氧化物、铌氧化物中的一种或几种,以及铁族元素合金。其中,铁族元素合金可以直接销售给炼钢企业。具体的,铁族元素合金在底部,而且稀土氧化物较为松散,进行剥离即可分离。Step (5): Separate the cooled material in step (4) to obtain rare earth oxides, trace amounts of one or more of aluminum oxides, titanium oxides, niobium oxides, and iron group element alloys . Among them, iron group element alloys can be sold directly to steelmaking companies. Specifically, the iron group element alloy is at the bottom, and the rare earth oxide is relatively loose and can be separated by peeling off.

具体的,碳首先选择稀土熔盐电解废阳极或废石墨槽。Specifically, the first choice for carbon is rare earth molten salt electrolysis waste anodes or waste graphite tanks.

具体的,碳还可选装高炉焦、沥青焦或木炭。Specifically, the carbon can also be equipped with blast furnace coke, pitch coke or charcoal.

具体的,步骤(1)中粉碎后的处理物料的粒度小于0.061mm(250目)。Specifically, the particle size of the processed material after crushing in step (1) is less than 0.061 mm (250 mesh).

具体的,至少含有稀土元素与铁族元素的处理物料为已经去除过油污及将杂质降低至合适水平的物料。Specifically, the treated materials containing at least rare earth elements and iron group elements are materials that have removed oil stains and reduced impurities to appropriate levels.

具体的,氧化装置可选自气氛保护回转窑,气氛炉或隧道窑。Specifically, the oxidation device can be selected from an atmosphere protected rotary kiln, an atmosphere furnace or a tunnel kiln.

具体的,熔炼装置可选自中频炉,工频炉,高频感应炉。Specifically, the smelting device can be selected from medium frequency furnaces, power frequency furnaces, and high frequency induction furnaces.

具体的,所述磁性材料废料包含镧、铈、镨、钕、钐、铕、钆、铽、镝、钬、铒、铥、镱、镥、钪和钇中的一种或多种稀土元素。Specifically, the magnetic material waste includes one or more rare earth elements among lanthanum, cerium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, scandium and yttrium.

具体的,所述中还原后的氧化物粉碎后的处理物料的粒度小于0.061mm(250目)。Specifically, the particle size of the processed material after the reduced oxide is crushed is less than 0.061 mm (250 mesh).

本发明上述内容提供了一种稀土磁性材料废料中全稀土元素回收方法。本发明设计的具有特定工艺路线和工艺参数的回收方法是一种充分利用稀土磁性材料废料中的金属,实现全部回收利用稀土磁性材料中的金属的处理稀土磁性材料废料的方法。本发明可以从稀土磁性材料废料回收稀土氧化物及其它金属,该方法操作简单,低成本、无酸碱连续循环、无废弃物、适合连续作业。The above content of the present invention provides a method for recovering all rare earth elements in rare earth magnetic material waste. The recycling method with specific process routes and process parameters designed by the present invention is a method for processing rare earth magnetic material waste that fully utilizes the metal in the rare earth magnetic material waste and realizes the full recovery and utilization of the metal in the rare earth magnetic material. The invention can recover rare earth oxides and other metals from rare earth magnetic material waste. The method has simple operation, low cost, no acid and alkali continuous circulation, no waste, and is suitable for continuous operation.

本发明通过先对物料进行除杂、粉碎、氧化处理,将稀土金属及铁等金属转为氧化物,通过碳还原体将铁、铜等的氧化物还原为金属,金属处于液态,氧化物处于固态,浇注入模具,冷却后通过物理方法将金属与氧化物进行有效分离。本发明通过该回收工艺可实现对稀土磁性材料废料中金属的全回收利用,而且操作简单方便,工艺连续可控,低成本、不需要使用酸碱,不产生废水,不排放有毒气体,无废弃物,对环境污染极少,适合连续作业,更加适于规模化工业生产的推广和应用。This invention first removes impurities, crushes and oxidizes the materials, converts rare earth metals, iron and other metals into oxides, and reduces the oxides of iron, copper, etc. into metals through carbon reducers. The metals are in a liquid state and the oxides are in a liquid state. In solid state, it is poured into a mold, and after cooling, the metal and oxide are effectively separated by physical methods. The present invention can realize full recycling of metals in rare earth magnetic material waste through this recycling process, and the operation is simple and convenient, the process is continuously controllable, low cost, does not require the use of acids and bases, does not produce waste water, does not emit toxic gases, and has no waste. It has very little environmental pollution, is suitable for continuous operation, and is more suitable for the promotion and application of large-scale industrial production.

实验结果表明,采用本发明提供的从稀土材料废料中全稀土元素回收方法,收率大于92.5%,大于行业的90%,而且回收路径简单,无废弃物产生,成本低。Experimental results show that using the method for recovering all rare earth elements from rare earth material waste provided by the present invention, the yield is greater than 92.5%, which is greater than 90% of the industry, and the recovery path is simple, no waste is generated, and the cost is low.

为了进一步说明本发明,以下结合实施例对本发明提供的一种稀土磁性材料废料中全稀土元素回收方法进行详细描述,但是应当理解,这些实施例是在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,只是为进一步说明本发明的特征和优点,而不是对本发明权利要求的限制,本发明的保护范围也不限于下述的实施例。In order to further illustrate the present invention, a method for recovering all rare earth elements from rare earth magnetic material waste provided by the present invention is described in detail below with reference to the examples. However, it should be understood that these examples are implemented based on the technical solution of the present invention. Detailed embodiments and specific operating procedures are given only to further illustrate the features and advantages of the present invention, but are not intended to limit the claims of the present invention, and the protection scope of the present invention is not limited to the following examples.

实施例1Example 1

对于R-Fe-B超细粉使用回转窑进行燃烧处理,800℃保温120分钟,物料被氧化成氧化物,其中铁的氧化物质量占49.3%。将氧化后的物料与碳粉(灰分含量小于1%)混匀,碳与铁氧化物的质量比为1:6.0。将混匀后的物料加入中频炉,在大气环境中升温,并在1350℃处理30分钟。将物料倒入浇铸钢包并迅速冷却至200℃以下。冷却至室温后将金属块及金属颗粒与其它物料分离。The R-Fe-B ultrafine powder is burned in a rotary kiln and kept at 800°C for 120 minutes. The material is oxidized into oxides, of which the mass of iron oxides accounts for 49.3%. Mix the oxidized material and carbon powder (ash content less than 1%) evenly. The mass ratio of carbon to iron oxide is 1:6.0. Add the mixed materials into the intermediate frequency furnace, raise the temperature in the atmospheric environment, and treat it at 1350°C for 30 minutes. Pour the material into the casting ladle and quickly cool it to below 200°C. After cooling to room temperature, the metal blocks and metal particles are separated from other materials.

本发明实施例1中,投入氧化物102kg,还原后得金属35.76kg,氧化物48.93kg。稀土元素收率95.15%。In Example 1 of the present invention, 102kg of oxide was put in, and after reduction, 35.76kg of metal and 48.93kg of oxide were obtained. The yield of rare earth elements is 95.15%.

金属使用ICP-AES测稀土元素含量,氧化物中铁含量使用GB/T 12690.6——2017标准方法测定,C使用碳硫仪测定。The content of rare earth elements in metals was measured using ICP-AES, the content of iron in oxides was measured using the GB/T 12690.6-2017 standard method, and C was measured using a carbon-sulfur meter.

参见表1,表1为本发明实施例1中稀土氧化物和金属合金中的主要元素含量分析。See Table 1. Table 1 is an analysis of the main element contents in the rare earth oxides and metal alloys in Example 1 of the present invention.

表1Table 1

项目project FeFe PrPr NdNd GdGd AlAl CC 相APhase A 99.599.5 0.010.01 0.010.01 00 0.420.42 0.250.25 相BPhase B 2.222.22 19.4119.41 77.6277.62 0.4830.483 0.0760.076 0.010.01

实施例2Example 2

对于R-Fe-B不规则块料先用高速破碎机破碎成小于0.061mm的物料,然后使用回转窑进行燃烧处理,800℃保温120分钟,物料被氧化成氧化物,其中铁的氧化物质量占69.89%。取氧化后的物料20kg与2.33Kg石墨粉混匀,然后分三次加入中频炉,熔炼210分钟。将熔炼后的物料倒入浇注模具(模具需水冷),冷却至接近室温后将金属块与其它物料分离。For R-Fe-B irregular block materials, first use a high-speed crusher to break into materials smaller than 0.061mm, and then use a rotary kiln for combustion treatment. The materials are kept at 800°C for 120 minutes. The materials are oxidized into oxides, among which the mass of iron oxides Accounting for 69.89%. Take 20kg of the oxidized material and mix it with 2.33Kg of graphite powder, then add it to the intermediate frequency furnace in three batches and smelt for 210 minutes. Pour the smelted material into the pouring mold (the mold needs to be water-cooled), and then separate the metal block from other materials after cooling to close to room temperature.

本发明实施例2中,熔炼后得金属12.9kg,氧化物8.02kg。稀土元素收率93.5%。In Example 2 of the present invention, 12.9 kg of metal and 8.02 kg of oxide were obtained after smelting. The rare earth element yield is 93.5%.

参见表2,表2为本发明实施例2中稀土氧化物和金属合金中的主要元素含量分析。See Table 2. Table 2 is an analysis of the main element contents in the rare earth oxides and metal alloys in Example 2 of the present invention.

表2Table 2

项目project FeFe PrPr NdNd CeCe GdGd AlAl CC 相APhase A 99.599.5 0.010.01 0.010.01 0.010.01 00 0.020.02 0.2370.237 相BPhase B 3.523.52 16.4116.41 51.2151.21 28.228.2 0.4830.483 0.1960.196 0.0350.035

实施例3Example 3

对于R-Fe-B磨削粉先通过磁选机选除非金属氧化物,然后使用回转窑进行燃烧处理,850℃保温120分钟,物料被氧化成氧化物,其中铁的氧化物质量占69.5%。去氧化后的物料20kg与2.0石墨粉混匀,分三次加入50kg中频炉中,熔炼180分钟,然后将物料倒入钢包(水冷却),冷却至近室温后将金属块、金属颗粒与其它物料分离。For R-Fe-B grinding powder, non-metallic oxides are first selected through a magnetic separator, and then burned in a rotary kiln. The material is kept at 850°C for 120 minutes, and the material is oxidized into oxides, of which the mass of iron oxides accounts for 69.5%. . Mix 20kg of deoxidized material with 2.0 graphite powder, add it to a 50kg intermediate frequency furnace in three batches, and smelt for 180 minutes. Then pour the material into a ladle (water cooling). After cooling to near room temperature, separate the metal blocks, metal particles and other materials. .

本发明实施例3中,熔炼后得金属12.54kg,氧化物8.52kg。稀土元素收率92.57%。In Example 3 of the present invention, 12.54kg of metal and 8.52kg of oxide were obtained after smelting. The yield of rare earth elements is 92.57%.

参见表3,表3为本发明实施例3中稀土氧化物和金属合金中的主要元素含量分析。See Table 3. Table 3 is an analysis of the main element contents in the rare earth oxides and metal alloys in Example 3 of the present invention.

表3table 3

项目project FeFe PrPr NdNd CeCe GdGd SiSi CC 相APhase A 99.599.5 0.010.01 0.010.01 0.010.01 00 0.0320.032 0.1780.178 相BPhase B 4.574.57 16.4016.40 51.2251.22 26.726.7 0.4830.483 0.0460.046 0.0550.055

以上对本发明提供的一种稀土磁性材料废料中全稀土元素回收方法进行了详细的介绍,本文中应用了具体个例对本发明的原理及实施方式进行了阐述,以上实施例的说明只是用于帮助理解本发明的方法及其核心思想,包括最佳方式,并且也使得本领域的任何技术人员都能够实践本发明,包括制造和使用任何装置或系统,和实施任何结合的方法。应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以对本发明进行若干改进和修饰,这些改进和修饰也落入本发明权利要求的保护范围内。本发明专利保护的范围通过权利要求来限定,并可包括本领域技术人员能够想到的其他实施例。如果这些其他实施例具有不是不同于权利要求文字表述的结构要素,或者如果它们包括与权利要求的文字表述无实质差异的等同结构要素,那么这些其他实施例也应包含在权利要求的范围内。The above is a detailed introduction to the method for recovering all rare earth elements in rare earth magnetic material waste provided by the present invention. Specific examples are used in this article to illustrate the principles and implementation methods of the present invention. The description of the above examples is only for assistance. An understanding of the methods and core concepts of the invention, including the best mode, and also enables any person skilled in the art to practice the invention, including making and using any devices or systems and performing any combined methods. It should be noted that those skilled in the art can make several improvements and modifications to the present invention without departing from the principles of the present invention, and these improvements and modifications also fall within the scope of the claims of the present invention. The scope of patent protection of the present invention is defined by the claims, and may include other embodiments that occur to those skilled in the art. These other embodiments shall also be included within the scope of the claims if they have structural elements that do not differ from the literal expressions of the claims, or if they include equivalent structural elements with insubstantial differences from the literal expressions of the claims.

Claims (10)

1.一种稀土磁性材料废料中全稀土元素回收方法,其特征在于,包括以下步骤:1. A method for recovering all rare earth elements from rare earth magnetic material waste, which is characterized by comprising the following steps: 1)将稀土磁性材料废料进行粉碎和燃烧氧化后,得到充分氧化物;1) After crushing, burning and oxidizing the rare earth magnetic material waste, sufficient oxides are obtained; 2)将上述步骤得到的充分氧化物与碳混合,经过热处理还原后,然后进行冷却,分离后得到金属物料和稀土氧化物。2) Mix the sufficient oxides obtained in the above steps with carbon, reduce them through heat treatment, then cool them, and then separate them to obtain metal materials and rare earth oxides. 2.根据权利要求1所述的回收方法,其特征在于,所述粉碎后的稀土磁性材料废料的粒度小于等于0.061mm;2. The recycling method according to claim 1, characterized in that the particle size of the crushed rare earth magnetic material waste is less than or equal to 0.061 mm; 所述燃烧氧化的方式在含氧气氛下进行燃烧氧化;The combustion oxidation method carries out combustion oxidation in an oxygen-containing atmosphere; 所述含氧气氛的氧气体积含量为4%~21%。The oxygen volume content of the oxygen-containing atmosphere is 4% to 21%. 3.根据权利要求1所述的回收方法,其特征在于,所述燃烧氧化的温度为大于等于500℃;3. The recycling method according to claim 1, characterized in that the temperature of the combustion and oxidation is greater than or equal to 500°C; 所述燃烧氧化的时间为12~24h。The combustion and oxidation time is 12 to 24 hours. 4.根据权利要求1所述的回收方法,其特征在于,所述稀土磁性材料废料中包含镧、铈、镨、钕、钐、铕、钆、铽、镝、钬、铒、铥、镱、镥、钪和钇中的一种或多种稀土元素;4. The recycling method according to claim 1, characterized in that the rare earth magnetic material waste contains lanthanum, cerium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, one or more rare earth elements from the group consisting of lutetium, scandium and yttrium; 所述充分氧化物与碳的质量比为,以充分氧化物中的Fe元素计,Fe与碳的质量比为(2.4~2.8):1;The mass ratio of the sufficient oxide to carbon is, based on the Fe element in the sufficient oxide, the mass ratio of Fe to carbon is (2.4-2.8): 1; 所述碳包括高炉焦、沥青焦和木炭中的一种或多种。The carbon includes one or more of blast furnace coke, pitch coke and charcoal. 5.根据权利要求1所述的回收方法,其特征在于,所述碳包括稀土熔盐电解废阳极和/或废石墨槽;5. The recycling method according to claim 1, wherein the carbon includes waste rare earth molten salt electrolysis anodes and/or waste graphite tanks; 所述热处理还原的温度为大于等于710℃;The temperature of the heat treatment reduction is greater than or equal to 710°C; 所述热处理还原的时间为4~6h。The heat treatment reduction time is 4 to 6 hours. 6.根据权利要求1所述的回收方法,其特征在于,所述分离的方式包括剥离;6. The recycling method according to claim 1, characterized in that the separation method includes stripping; 所述冷却后,得到的物料中,稀土氧化物位于物料上层;After the cooling, in the obtained material, the rare earth oxide is located in the upper layer of the material; 所述稀土氧化物具有松散的团状结构。The rare earth oxide has a loose mass structure. 7.根据权利要求1所述的回收方法,其特征在于,所述稀土氧化物中还包括碳、铝氧化物、钛氧化物、铌氧化物和铁氧化物中的一种或多种;7. The recycling method according to claim 1, wherein the rare earth oxide further includes one or more of carbon, aluminum oxide, titanium oxide, niobium oxide and iron oxide; 所述铝氧化物在稀土氧化物中的质量含量为0.1%~0.5%。The mass content of the aluminum oxide in the rare earth oxide is 0.1% to 0.5%. 8.根据权利要求7所述的回收方法,其特征在于,所述钛氧化物在稀土氧化物中的质量含量为0.03%~0.10%;8. The recycling method according to claim 7, characterized in that the mass content of the titanium oxide in the rare earth oxide is 0.03% to 0.10%; 所述铌氧化物在稀土氧化物中的质量含量为0.03%~0.3%;The mass content of the niobium oxide in the rare earth oxide is 0.03% to 0.3%; 所述铁氧化物在稀土氧化物中的质量含量为0.3%~10%。The mass content of the iron oxide in the rare earth oxide is 0.3% to 10%. 9.根据权利要求1所述的回收方法,其特征在于,所述金属物料包括铁族元素合金;9. The recycling method according to claim 1, wherein the metal material includes an alloy of iron group elements; 所述金属物料还包括稀土元素、铝元素和碳元素中的一种或多种。The metal material also includes one or more of rare earth elements, aluminum elements and carbon elements. 10.根据权利要求9所述的回收方法,其特征在于,所述稀土元素在金属物料中的质量含量为90%~99.5%;10. The recycling method according to claim 9, characterized in that the mass content of the rare earth elements in the metal material is 90% to 99.5%; 所述铝元素在金属物料中的质量含量为0.03%~0.10%;The mass content of the aluminum element in the metal material is 0.03% to 0.10%; 所述碳元素在金属物料中的质量含量为0.005%~0.1%。The mass content of the carbon element in the metal material is 0.005% to 0.1%.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002060863A (en) * 2000-08-22 2002-02-28 Shin Etsu Chem Co Ltd Recovery method of rare earth elements from sludge containing rare earth elements
CN102978401A (en) * 2012-11-26 2013-03-20 沈少波 Method for recovering rare earth and other metals from neodymium iron boron and samarium cobalt magnetic material waste
CN106133157A (en) * 2014-03-28 2016-11-16 日立金属株式会社 The recovery method of rare earth element
CN112553482A (en) * 2020-10-13 2021-03-26 赣州蓝海新材料有限公司 Method for efficiently extracting iron from neodymium iron boron waste to enrich rare earth elements
CN114540625A (en) * 2022-02-28 2022-05-27 开化祥盛磁业有限公司 Method for recovering rare earth oxide by using rare earth magnetic material waste

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002060863A (en) * 2000-08-22 2002-02-28 Shin Etsu Chem Co Ltd Recovery method of rare earth elements from sludge containing rare earth elements
CN102978401A (en) * 2012-11-26 2013-03-20 沈少波 Method for recovering rare earth and other metals from neodymium iron boron and samarium cobalt magnetic material waste
CN106133157A (en) * 2014-03-28 2016-11-16 日立金属株式会社 The recovery method of rare earth element
CN112553482A (en) * 2020-10-13 2021-03-26 赣州蓝海新材料有限公司 Method for efficiently extracting iron from neodymium iron boron waste to enrich rare earth elements
CN114540625A (en) * 2022-02-28 2022-05-27 开化祥盛磁业有限公司 Method for recovering rare earth oxide by using rare earth magnetic material waste

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