JPH1074539A - Method for recovering reusable material from used lithium battery - Google Patents

Method for recovering reusable material from used lithium battery

Info

Publication number
JPH1074539A
JPH1074539A JP23167996A JP23167996A JPH1074539A JP H1074539 A JPH1074539 A JP H1074539A JP 23167996 A JP23167996 A JP 23167996A JP 23167996 A JP23167996 A JP 23167996A JP H1074539 A JPH1074539 A JP H1074539A
Authority
JP
Japan
Prior art keywords
magnetic material
magnetic
roasting
crushing
separated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP23167996A
Other languages
Japanese (ja)
Other versions
JP3079285B2 (en
Inventor
Yoichi Takazawa
洋一 高沢
Takehisa Aoki
威尚 青木
Nihachi Sonoda
二八 園田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nikko Kinzoku KK
Original Assignee
Nikko Kinzoku KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nikko Kinzoku KK filed Critical Nikko Kinzoku KK
Priority to JP23167996A priority Critical patent/JP3079285B2/en
Publication of JPH1074539A publication Critical patent/JPH1074539A/en
Application granted granted Critical
Publication of JP3079285B2 publication Critical patent/JP3079285B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/54Reclaiming serviceable parts of waste accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/84Recycling of batteries or fuel cells

Abstract

PROBLEM TO BE SOLVED: To recover reusable material by one crushing by roasting used lithium batteries, crushing, and magnetically separating a magnetic material and a non-magnetic material. SOLUTION: Used lithium battery raw material 1 is roasted with a roasting furnace 3, crushed with a crushing machine 2 in to the dimensions suitable for magnetic separation. A magnetic material in the crushed materials is separated from a non-magnetic material with a magnetic separator 7, then they are separately sieved with a sieving machine 8. In the roasting of the raw material 1, an organic material is decomposed, burned, and vaporized to generate CO gas. In low temperature roasting, reduction of metallic lithium by CO gas is insufficient, load in rushing is made large, and in high temperature roasting, the raw material 1 is melted and coagulated to make crushing difficult. Roasting at 800-1000 deg.C is preferable. The magnetic material and the non-magnetic material are magnetically separated, the magnetic material is used as a heat resistant alloy material and the non-magnetic material is used as the raw material of copper. In the sieving machine 8, the magnetic material is separated into powdery cobalt and plate-shaped or block iron component, and the non-magnetic material is separated into foil-shaped copper and powdery aluminum. Reusable materials are recovered and load in crushing is lightened.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は使用済みリチウム電
池からの有価物回収方法に関するものである。リチウム
電池は、小型、軽量、体積当りのエネルギ密度大などの
特長を有しているために、携帯電話、PHS,ビデオカ
メラ、ノートパソコンなどの電源として使用されてい
る。
The present invention relates to a method for recovering valuable resources from a used lithium battery. Lithium batteries are used as power sources for mobile phones, PHSs, video cameras, notebook computers, and the like because of their features such as small size, light weight, and high energy density per volume.

【0002】リチウム電池の主たる構成部品は、鋼製ケ
ース、銅箔からなる負極極板、アルミ箔に金属酸リチウ
ム(金属=Mo,Co,Niなど)を塗布した正極板、
ポリエチレン等からなるセパレータなどである。金属酸
リチウムに含まれているMo,Co,Niなどは有価金
属であるために、幾つかの回収方法が提案されている。
The main components of a lithium battery are a steel case, a negative electrode plate made of copper foil, a positive electrode plate made of aluminum foil coated with lithium metal oxide (metal = Mo, Co, Ni, etc.),
Examples include a separator made of polyethylene or the like. Since Mo, Co, Ni and the like contained in lithium metal oxide are valuable metals, some recovery methods have been proposed.

【0003】[0003]

【従来の技術】特開平6−322452号公報による
と、使用済みリチウム二次電池の破砕物を磁選して分別
された金属ニッケルなどの磁性物を除いた破砕物を非酸
化性雰囲気で焙焼しもしくは還元性雰囲気で還元焙焼
し、得られた焙焼物を磁選することが提案されている。
上記方法における非酸化性雰囲気中での焙焼はセパレー
ター、負極材の炭素などとして含まれている炭素質物質
により金属酸化物を還元するための工程であり、また、
最後の磁選はニッケル、コバルトを銅などより分離する
ための工程である。
2. Description of the Related Art According to Japanese Patent Application Laid-Open No. 6-322452, a crushed product of a used lithium secondary battery, which is separated by magnetic separation from magnetic materials such as metallic nickel, is roasted in a non-oxidizing atmosphere. Or reduction roasting in a reducing atmosphere and subjecting the resulting roasted product to magnetic separation have been proposed.
Roasting in a non-oxidizing atmosphere in the above method is a step for reducing the metal oxide by a carbonaceous substance contained as separator, carbon of the negative electrode material, etc.,
The last magnetic separation is a process for separating nickel and cobalt from copper and the like.

【0004】特開平6−346160号公報によると、
使用済みリチウム二次電池を焙焼することによって結着
剤、溶剤などを除去し、焙焼物を破砕し、篩別して篩下
を製錬の原料とすることが提案されている。
According to Japanese Patent Application Laid-Open No. 6-346160,
It has been proposed that a used lithium secondary battery is roasted to remove a binder, a solvent, and the like, and the roasted product is crushed and sieved to use the sieved material as a raw material for smelting.

【0005】[0005]

【発明が解決しようとする課題】前掲特開平6−322
452号公報では、使用済みリチウム二次電池を直接破
砕しているが、この破砕は焙焼物の破砕と比べて困難で
ある。さらに、焙焼の負担を軽減するために、焙焼経ず
に破砕物を直接磁選しているために、非磁性物と磁性物
を分離する磁選が焙焼前後で2回行われている。次に、
特開平6−346160号公報の方法ではNi,Coの
回収は製錬工程に委ねられるために、熱エネルギの面で
改善の余地がある。
Problems to be Solved by the Invention JP-A-6-322, cited above.
In Japanese Patent No. 452, a used lithium secondary battery is directly crushed, but this crushing is more difficult than crushing of a roasted product. Further, in order to reduce the burden of roasting, since the crushed material is directly magnetically separated without roasting, magnetic separation for separating a non-magnetic material and a magnetic material is performed twice before and after roasting. next,
In the method disclosed in JP-A-6-346160, the recovery of Ni and Co is left to the smelting process, so there is room for improvement in terms of thermal energy.

【0006】[0006]

【課題を解決するための手段】本発明は、粉砕を容易に
しかつ1回の磁選で済むような方法で使用済みリチウム
電池から有価金属を回収することを目的としており、使
用済みリチウム電池を焙焼し、得られた焙焼物を破砕
し、磁選して磁性物と非磁性物に分別することを特徴と
している。以下、本発明の方法を詳しく説明する。
SUMMARY OF THE INVENTION An object of the present invention is to recover valuable metals from used lithium batteries by a method that facilitates pulverization and requires only one magnetic separation. It is characterized by baking, crushing the obtained roasted product, and magnetically separating it into a magnetic material and a non-magnetic material. Hereinafter, the method of the present invention will be described in detail.

【0007】まず、本発明の方法においては使用済みリ
チウム電池を焙焼することによって、ポリプロピレン、
n−メチル−2−ピロリドンなどの有機物を分解、燃
焼、揮発させるとともに還元ガスとなるCOを発生させ
る。焙焼温度は低過ぎると、有機物の分解により発生す
るCOガスによる金属酸リチウムの還元が不充分とな
り、かつ破砕の負担が大きくなり、一方高過ぎると焙焼
物が溶融凝固してその破砕が困難になり、また銅の溶融
が起こり炉を破損するので、550〜1100℃が好ま
しく、より好ましくは800〜1000℃である。
First, in the method of the present invention, a spent lithium battery is roasted to obtain polypropylene,
Organic substances such as n-methyl-2-pyrrolidone are decomposed, burned and volatilized, and CO as a reducing gas is generated. If the roasting temperature is too low, the reduction of lithium metal oxide by the CO gas generated by decomposition of organic matter becomes insufficient and the burden of crushing increases, while if it is too high, the roasted material melts and solidifies and its crushing is difficult. 550 to 1100 ° C., more preferably 800 to 1000 ° C., because melting of copper occurs and the furnace is damaged.

【0008】焙焼のための加熱炉は限定はされないが、
電気炉、重油炉などの定置炉で行うことができる。この
場合ストーカ下直火加熱定置炉を使用することができ
る。使用済みリチウム電池は1バッチ分をストーカ上に
積上げ、炉の上部からは燃焼排ガスの煙道を設けて、燃
焼ガスを適宜排出しながら焙焼を行う。使用済みリチウ
ム電池を破砕せずに焙焼した場合は、電池内部で上記し
た有機物の燃焼、COガスの発生などが起こり、電池の
ケース内の空間で酸化物の還元が進む。この焙焼により
酸化鉄、酸化ニッケル、酸化コバルトなどはほとんどが
還元され、一方銅箔などは金属形態を保っている。アル
ミは溶融して何れかの粉、塊などに薄く付着している。
得られる焙焼物は使用済みリチウム電池に対して約70
〜90重量%の金属粉、塊、ネット、箔、板あるいはこ
れらが電池内の結合構造を一部維持しているものとな
る。金属の他に若干の未燃焼炭素、有機物なども含まれ
る。
[0008] The heating furnace for roasting is not limited,
It can be performed in a stationary furnace such as an electric furnace or a heavy oil furnace. In this case, a direct heating furnace under a stoker can be used. One batch of used lithium batteries is stacked on a stoker, and a flue of combustion exhaust gas is provided from the upper part of the furnace, and roasting is performed while appropriately discharging combustion gas. When the used lithium battery is roasted without being crushed, the above-described burning of organic substances and generation of CO gas occur inside the battery, and the reduction of oxide proceeds in the space in the battery case. This roasting reduces most of iron oxide, nickel oxide, cobalt oxide and the like, while copper foil and the like maintain a metal form. Aluminum is melted and thinly attached to any powder, lump or the like.
The obtained roasted product is about 70% for the used lithium battery.
Up to 90% by weight of metal powder, lump, net, foil, plate or these partially maintain the bonding structure in the battery. In addition to metals, some unburned carbon and organic substances are also included.

【0009】次に、焙焼物の破砕を行う。この破砕は上
記した種々の形態を有し、また寸法がまちまちな焙焼物
を適度の寸法に揃え、電池の構造を維持しているものは
粉末、板、箔などの素材形態まで分離し、次の磁選で磁
性物と被磁性物とに分離し易くする操作である。破砕機
としては、限定されるものではないが、一軸破砕機など
を好ましく使用することができる。また破砕はJIS
Z 8801の標準篩で20mm未満となるようにする
ことが好ましい。本発明法による焙焼後破砕では、電池
自体を直接破砕するのではなく焙焼により一旦ある程度
破砕されかつ重量が減っている電池を破砕するために、
破砕の負担が軽減されている。また焙焼物はほとんどの
割合が金属であり、破砕が困難な炭素、有機物がほとん
どないために、この面でも破砕の負担が軽減される。
Next, the roasted material is crushed. This crushing has various forms as described above, and also prepares roasted products of various sizes to an appropriate size, and those that maintain the structure of the battery are separated into powder, plate, foil and other material forms. This operation facilitates separation into a magnetic substance and a magnetic substance in the magnetic separation. The crusher is not limited, but a single-shaft crusher or the like can be preferably used. The crushing is JIS
It is preferred to make the standard sieve of Z8801 less than 20 mm. In the crushing after roasting according to the method of the present invention, instead of directly crushing the battery itself, in order to crush the battery once crushed to some extent and reduced in weight by roasting,
The crushing burden is reduced. In addition, since the roasted product is almost entirely composed of metal and hardly contains carbon and organic substances that are difficult to crush, the burden of crushing is also reduced in this aspect.

【0010】本発明の最後の工程では磁選を行う。これ
は磁性物である金属リチウム酸塩の焙焼物及びケースな
どの鉄の焙焼物を非磁性物から分別するための工程であ
る。焙焼中には金属リチウム酸塩を担持するアルミ箔が
溶融するので、コバルトとアルミの合金が生成している
のではないかと考えられたが、意外にもアルミは負極材
料である銅箔と一体になっている割合が多いことが分か
った。したがって、磁選により分別される磁性物にはア
ルミが少ない。以上のようにして得られる磁性物はその
まま耐熱合金などの原料とすることができる。非磁性物
は銅の原料とすることができる。
In the last step of the present invention, magnetic separation is performed. This is a step for separating a roasted metal lithium salt and a roasted iron such as a case, which are magnetic substances, from non-magnetic substances. During the roasting, the aluminum foil supporting the metal lithium salt melted, so it was thought that an alloy of cobalt and aluminum might have been formed. It turned out that there was a lot of unity. Therefore, there is little aluminum in the magnetic material separated by magnetic separation. The magnetic material obtained as described above can be used as a raw material such as a heat-resistant alloy. The non-magnetic material can be a raw material for copper.

【0011】さらに、Feリッチ分とCoリッチを分離
することが必要な場合は磁性物を,好ましくはJIS
Z 8801の標準篩で420〜5000μm未満と以
上に篩別すると、篩上は鉄スクラップとなり、篩下はコ
バルト原料として分別される。このような分別が可能で
あるのは、焙焼後の破砕物ではコバルトは概して粉末状
であり、鉄は概して板、塊状であることによる。同様
に、非磁性物中のCuリッチ分とAlリッチ分を分離す
ることが必要な場合は、非磁性物を,好ましくは、JI
S Z 8801の標準篩で420〜5000μm未満
と以上に篩別すると篩上は前者となり、篩下は後者とな
る。このように分別が可能であるのは、焙焼後の破砕物
では銅は概して箔状であり、アルミは概して粒状である
ためである。以上のCoに関する説明はNiと置き換え
ても全く同じことである。すなわち、Niは磁性物であ
るのでCoと同様の方法で回収することができる。
Further, if it is necessary to separate the Fe-rich component and the Co-rich component, a magnetic material, preferably JIS
When sieving with a standard sieve of Z8801 to 420 to less than 5000 μm or more, the upper part of the screen becomes iron scrap, and the lower part is separated as a cobalt raw material. Such a separation is possible because, in the crushed material after roasting, cobalt is generally in a powdery state, and iron is generally in a plate or lump. Similarly, when it is necessary to separate the Cu-rich portion and the Al-rich portion in the non-magnetic material, the non-magnetic material is preferably separated by JI.
When sieving with a standard sieve of SZ8801 to 420 to less than 5000 μm, the upper sieve becomes the former and the lower sieve becomes the latter. Such separation is possible because, in the crushed material after roasting, copper is generally in a foil shape and aluminum is generally in a granular shape. The above description regarding Co is exactly the same even if it is replaced with Ni. That is, since Ni is a magnetic substance, it can be recovered in the same manner as Co.

【0012】以下、本発明を実施するためのフローチャ
ートを参照してより具体的に説明する。使用済みリチウ
ム電池を原料1とし、電気炉もしくは重油炉などの焙焼
炉3に例えば400kg装入する。焙焼された有価金属
含有物が数トンに達したら破砕機2により磁選に適する
寸法への破砕を行う。破砕片は、2基のコンベヤと電磁
石を要素とする磁選機7により磁性物と非磁性物とに分
別される。磁性物及び非磁性物は篩別機8により、篩上
及び篩下に分別される。なお3は集塵設備、4は吸引フ
ァン、8はポータブルコンベアー、10は篩上コンテナ
バッグ、11は篩下コンテナバッグである。以下実施例
によりさらに詳しく本発明を説明する。
Hereinafter, the present invention will be described more specifically with reference to a flowchart for carrying out the present invention. A used lithium battery is used as a raw material 1, and 400 kg, for example, is charged into a roasting furnace 3 such as an electric furnace or a heavy oil furnace. When the roasted valuable metal content reaches several tons, the crusher 2 crushes it to a size suitable for magnetic separation. The crushed pieces are separated into a magnetic substance and a non-magnetic substance by a magnetic separator 7 having two conveyors and an electromagnet as elements. The magnetic substance and the non-magnetic substance are separated by the sieving machine 8 into upper and lower sieves. In addition, 3 is a dust collecting facility, 4 is a suction fan, 8 is a portable conveyor, 10 is a container bag above the sieve, and 11 is a container bag below the sieve. Hereinafter, the present invention will be described in more detail with reference to Examples.

【0013】[0013]

【実施例】原料の金属組成は下記のとおりであった。EXAMPLES The metal compositions of the raw materials were as follows.

【0014】[0014]

【表1】 [Table 1]

【0015】原料10tonを1000℃で1時間焙焼
したところ、2.2tonの重量減となったが、金属組
成は変化しなかった。次に磁選を行い磁性物6.0to
nと、非磁性物1.8tonを得た。それぞれの組成は
表2及び表3のとおりである。 (以下余白)
When 10 tons of the raw material was roasted at 1000 ° C. for 1 hour, the weight was reduced by 2.2 tons, but the metal composition did not change. Next, magnetic separation is performed and the magnetic material is 6.0 ton.
n and 1.8 ton of nonmagnetic material were obtained. The respective compositions are as shown in Tables 2 and 3. (Below)

【0016】[0016]

【表2】 [Table 2]

【0017】[0017]

【表3】 [Table 3]

【0018】続いて、磁性物を篩別機(5メッシュ)で
篩別し表4に示す篩上(3.2ton)及び表5に示す
篩下(3.0ton)を得た。 (以下余白)
Subsequently, the magnetic material was sieved with a sieving machine (5 mesh) to obtain a sieve (3.2 ton) shown in Table 4 and a sieve (3.0 ton) shown in Table 5. (Below)

【0019】[0019]

【表4】 [Table 4]

【0020】[0020]

【表5】 [Table 5]

【0021】また、非磁性物を同様に篩別機(5メッシ
ュ)で篩別し表6に示す篩上(1.4ton)及び表7
に示す篩下(0.4ton)を得た。 (以下余白)
The non-magnetic material was similarly sieved with a sieving machine (5 mesh), and sieved on a sieve (1.4 ton) shown in Table 6 and Table 7
(0.4 ton) was obtained. (Below)

【0022】[0022]

【表6】 [Table 6]

【0023】[0023]

【表7】 [Table 7]

【0024】以上説明したように本発明によると、Co
を磁性物の篩下として、Feを磁性物の篩上としてそれ
ぞれ回収することができる。また、銅はCuリッチなも
のは非磁性物の篩上として、Alリッチなものは非磁性
物の篩下として回収することができる。
As described above, according to the present invention, Co
Can be recovered under the magnetic material sieve, and Fe can be recovered as the magnetic material on the sieve. In addition, copper-rich copper can be recovered as a nonmagnetic material on a sieve, and Al-rich copper can be recovered as a nonmagnetic material under a sieve.

【0025】[0025]

【発明の効果】【The invention's effect】

(1)使用済みリチウム電池の1回の破砕で有価物を回
収することができる。 (2)使用済みリチウム電池の全量を破砕しないので破
砕の負担が軽減される。 (3)回収されたコバルト分は純度が38%以上である
ので、コバルト原料として使用可能である。なお少量の
アルミが随伴しているが、酸化により簡単に除去され
る。 (4)回収された鉄分はFe純度が高いために、あらゆ
る鉄源として使用可能である。 (5)非磁性物として回収された銅分は転炉、自溶炉な
どの銅製錬の原料となる。但し、Cuリッチ分とAlリ
ッチ分に分別することが好ましく、前者はPS転炉、後
者は自溶炉の原料とすることが製錬操業の面で好まし
い。 (6)上述のように有価金属純度がそれぞれの回収材料
中で高いにも拘らず、磁選が1回で済む。 (7)以上まとめると本発明方法を実施すると、ランニ
ングコストが少なく、破砕機及び磁選機も各1機で済む
ので設備投資コストも少なく、また回収材料も非常に価
値が高く、材料メーカー、鉄鋼メーカー、非鉄製錬業へ
の販売に適するものである。
(1) Valuables can be collected by one crushing of a used lithium battery. (2) Since the entire amount of the used lithium battery is not crushed, the burden of crushing is reduced. (3) Since the recovered cobalt content has a purity of 38% or more, it can be used as a cobalt raw material. Although a small amount of aluminum accompanies, it is easily removed by oxidation. (4) Since the recovered iron has high Fe purity, it can be used as any iron source. (5) Copper recovered as a non-magnetic material is used as a raw material for copper smelting in converters, flash smelting furnaces and the like. However, it is preferable to separate the mixture into a Cu-rich portion and an Al-rich portion. The former is preferably used as a raw material for a PS converter and the latter as a raw material for a flash smelting furnace in terms of smelting operation. (6) As described above, although the purity of the valuable metal is high in each recovered material, only one magnetic separation is required. (7) In summary, when the method of the present invention is carried out, running costs are low, and only one crusher and one magnetic separator are required, so that capital investment costs are low, and the recovered materials are very valuable. It is suitable for sale to manufacturers and non-ferrous smelters.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明法を実施する方法のフローシートであ
る。
FIG. 1 is a flow sheet of a method for carrying out the method of the present invention.

【符号の説明】[Explanation of symbols]

1 原料 3 焙焼炉 5 破砕機 7 磁選機 Reference Signs List 1 raw material 3 roasting furnace 5 crusher 7 magnetic separator

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 使用済みリチウム電池を焙焼し、得られ
た焙焼物を破砕し、磁選して磁性物と非磁性物に分別す
ることを特徴とする使用済みリチウム電池からの有価物
回収方法。
1. A method for recovering valuable resources from a used lithium battery, comprising roasting a used lithium battery, crushing the obtained roasted product, and magnetically separating the obtained product from a magnetic material and a non-magnetic material. .
【請求項2】 前記磁選により分別された磁性物を篩別
して主として鉄屑からなる篩上と、主としてコバルトか
らなる篩下とに分別することを特徴とする請求項1記載
の使用済みリチウム電池からの有価物回収方法。
2. The used lithium battery according to claim 1, wherein the magnetic material separated by the magnetic separation is sieved to be separated into an upper sieve mainly composed of iron chips and a lower sieve mainly composed of cobalt. Valuable resources recovery method.
【請求項3】 前記磁選により分別された非磁性物を篩
別してアルミリッチな篩下と銅リッチな篩上に分別する
ことを特徴とする請求項1又は2記載の使用済リチウム
電池からの有価物回収方法。
3. The valuable lithium battery according to claim 1, wherein the non-magnetic material separated by the magnetic separation is sieved to be separated into an aluminum-rich sieve and a copper-rich sieve. Object collection method.
JP23167996A 1996-09-02 1996-09-02 How to recover valuable resources from used lithium batteries Expired - Fee Related JP3079285B2 (en)

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Application Number Priority Date Filing Date Title
JP23167996A JP3079285B2 (en) 1996-09-02 1996-09-02 How to recover valuable resources from used lithium batteries

Publications (2)

Publication Number Publication Date
JPH1074539A true JPH1074539A (en) 1998-03-17
JP3079285B2 JP3079285B2 (en) 2000-08-21

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ID=16927296

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Country Link
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JPH11185833A (en) * 1997-12-25 1999-07-09 Nippon Mining & Metals Co Ltd Valuable material recovering method from used lithium battery
KR100425554B1 (en) * 2001-09-18 2004-04-03 한국지질자원연구원 High-temperature Treatment to recover Valuable Metals from Spent Lithium Ion Batteries
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