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JP2866005B2 - Method for recovering valuable resources from discarded nickel-hydrogen storage alloy secondary batteries - Google Patents

Method for recovering valuable resources from discarded nickel-hydrogen storage alloy secondary batteries

Info

Publication number
JP2866005B2
JP2866005B2 JP15364394A JP15364394A JP2866005B2 JP 2866005 B2 JP2866005 B2 JP 2866005B2 JP 15364394 A JP15364394 A JP 15364394A JP 15364394 A JP15364394 A JP 15364394A JP 2866005 B2 JP2866005 B2 JP 2866005B2
Authority
JP
Japan
Prior art keywords
hydrogen storage
storage alloy
nickel
recovering valuable
secondary battery
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.)
Expired - Lifetime
Application number
JP15364394A
Other languages
Japanese (ja)
Other versions
JPH0820825A (en
Inventor
興士 笹井
昇 速水
勝 中村
洋司 見持
次徳 本多
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.)
NIPPON JUKAGAKU KOGYO KK
Original Assignee
NIPPON JUKAGAKU KOGYO 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
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Application filed by NIPPON JUKAGAKU KOGYO KK filed Critical NIPPON JUKAGAKU KOGYO KK
Priority to JP15364394A priority Critical patent/JP2866005B2/en
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Classifications

    • 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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • 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

Landscapes

  • Manufacture And Refinement Of Metals (AREA)
  • Secondary Cells (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、負極に水素吸蔵合金を
配したニッケル/アルカリ/水素吸蔵合金二次電池(本
明細書では以下Ni−MH電池と略記する)が使用済み
等のために廃棄された際に、この廃棄されたNi−MH
電池から有価物を回収する方法に関する。このNi−M
H電池の負極は、放電・充電に際して、M・H+OH-
⇔H2O+M+e-(但しMは水素吸蔵合金)の如くに反
応するが、充電(矢印←方向)の際に発生する水素ガス
は水素吸蔵合金Mに吸蔵されてM・Hとなるために、水
素分極を発生させる事がない。
BACKGROUND OF THE INVENTION The present invention relates to the use of a nickel / alkali / hydrogen storage alloy secondary battery (hereinafter abbreviated as Ni-MH battery in the present specification) having a hydrogen storage alloy in the negative electrode. When discarded, this discarded Ni-MH
The present invention relates to a method for recovering valuable resources from a battery. This Ni-M
When discharging / charging, the negative electrode of the H battery is MH + OH
反 応 H 2 O + M + e (where M is a hydrogen storage alloy), but the hydrogen gas generated during charging (in the direction of the arrow ←) is stored in the hydrogen storage alloy M and becomes M · H. Does not generate hydrogen polarization.

【0002】水素吸蔵合金としてはLaNi5系の合金
等の粉末が使用される。このNi−MH電池は、電気自
動車等の動力源に用いる二次電池として注目されてお
り、今後生産量の飛躍的な増加が見込まれている。
As a hydrogen storage alloy, a powder such as a LaNi 5 -based alloy is used. This Ni-MH battery is attracting attention as a secondary battery used for a power source of an electric vehicle or the like, and a dramatic increase in production is expected in the future.

【0003】[0003]

【従来の技術】Ni−MH電池は多孔質金属ニッケルま
たは繊維状金属ニッケルに水酸化ニッケルを充填した正
極と、ニッケルメッキした鉄のパンチングプレートや多
孔質金属ニッケル等に水素吸蔵合金粉末を導電材、バイ
ンダーとともに固着した負極と、ポリプロピレン等で形
成されたセパレーター等を有し、これ等は電解液ととも
に鋼製容器内に収納されて構成されている。
2. Description of the Related Art A Ni-MH battery has a positive electrode in which porous metal nickel or fibrous metal nickel is filled with nickel hydroxide, and a nickel-plated iron punching plate, porous metal nickel, or the like, and a hydrogen storage alloy powder as a conductive material. , A negative electrode fixed together with a binder, a separator formed of polypropylene or the like, and these are housed in a steel container together with the electrolytic solution.

【0004】このNi−MH電池は有害なカドミウムを
部材として使用していないために、ニッケル−カドミウ
ム電池とは異なり、廃棄しても深刻な公害を発生させる
ことがない。しかしニッケルや水素吸蔵合金は貴重な資
源であるために、廃棄されたNi−MH電池からこれ等
の有価物を回収する事は資源活用の観点から極めて重要
である。
Since this Ni-MH battery does not use harmful cadmium as a member, unlike a nickel-cadmium battery, it does not cause serious pollution even when disposed. However, since nickel and hydrogen storage alloys are valuable resources, it is extremely important to recover these valuable resources from discarded Ni-MH batteries from the viewpoint of resource utilization.

【0005】東北大学、素材工学研究所彙報48(19
92年12月)P.175には、ニッケル−水素電池の
ニッケルスクラップの中から、ニッケルおよびレアメタ
ル成分を、ハロゲン化揮発法やカルボニル法などの気相
反応を用いて分離回収する研究を開始した旨が記載され
ている。しかし具体的な技術内容は全く記載されていな
い。
[0005] Tohoku University, Institute of Materials Engineering, Bulletin 48 (19
(December 1992) On page 175, a study was started to separate and recover nickel and rare metal components from nickel scrap in nickel-hydrogen batteries using a gas phase reaction such as a halogenation volatilization method or a carbonyl method. Is described. However, no specific technical content is described.

【0006】JOM・1993,May,P32〜には、
負極にチタン系の水素吸蔵合金を配したニッケル-水素
二次電池の廃棄物全体を酸に溶解した結果が記載されて
いる。即ち硝酸に溶解し、その後溶解物を更に塩酸に溶
解すると、ニッケル分とチタン分を酸に溶解せしめ得る
ことが記載されている。しかしこの方法では水素吸蔵合
金も溶液となるために、回収物の価値は低く、また溶液
の後処理も複雑であると予想されるため、経済的な回収
法とはなり難い。
JOM 1993, May, P32-
It describes the result of dissolving the entire waste of a nickel-hydrogen secondary battery in which a titanium-based hydrogen storage alloy is disposed on the negative electrode in an acid. That is, it is described that when the substance is dissolved in nitric acid and then the dissolved substance is further dissolved in hydrochloric acid, the nickel and titanium components can be dissolved in the acid. However, in this method, since the hydrogen storage alloy also becomes a solution, the value of the recovered material is low, and the post-treatment of the solution is expected to be complicated, so that it is difficult to provide an economical recovery method.

【0007】[0007]

【発明が解決しようとする課題】上述したようにNi−
MH電池は、ニッケル、水酸化ニッケル、水素吸蔵合
金、セパレーター、合成樹脂フィルム、鋼製容器等の、
物理的・化学的特性が異なる多種類の部材で形成されて
いる。本発明はこの多種類の部材からなるNi−MH電
池の廃棄物から、簡易な方法でかつ高い価値を有する有
価物を回収する方法の提供を課題としている。
As described above, Ni-
MH batteries include nickel, nickel hydroxide, hydrogen storage alloys, separators, synthetic resin films, steel containers, etc.
It is formed of various types of members having different physical and chemical properties. It is an object of the present invention to provide a method for recovering valuable materials having a high value from a waste of Ni-MH batteries composed of various kinds of members by a simple method.

【0008】[0008]

【課題を解決するための手段および作用】本発明は、
(1)負極に粉末状水素吸蔵合金を配した、廃棄された
ニッケル−水素吸蔵合金二次電池から有価物を回収する
に際し、該二次電池を砕断し、砕断片を水中で処理して
粉末部をスラリーとし、ついでスラリー化しない部分と
スラリーとに分離し、スラリー化しない部分は鉄鋼原料
として回収し、スラリーは比重分離および/または浮遊
分離により粗水素吸蔵合金部と粗水酸化ニッケル部とに
分離し、粗水素吸蔵合金部は洗浄して水素吸蔵合金とし
て回収し、粗水酸化ニッケル部は酸溶解して不純物を除
去してニッケル化合物を回収することを特徴とする、廃
棄されたNi−MH電池から有価物を回収する方法であ
る。
SUMMARY OF THE INVENTION The present invention provides:
(1) When recovering valuable resources from a discarded nickel-hydrogen storage alloy secondary battery having a powdered hydrogen storage alloy disposed on the negative electrode, the secondary battery is crushed, and the crushed pieces are treated in water. The powder portion is converted into a slurry, and then a non-slurried portion is separated into a slurry and the non-slurried portion is recovered as a steel material. The slurry is separated by specific gravity and / or floating separation into a crude hydrogen storage alloy portion and a crude nickel hydroxide portion. The crude hydrogen storage alloy part was washed and recovered as a hydrogen storage alloy, and the crude nickel hydroxide part was dissolved in acid to remove impurities to recover nickel compounds, which was discarded. This is a method of recovering valuable resources from a Ni-MH battery.

【0009】また(2)砕断が、大気との接触を断って
行う砕断であることを特長とする、前記(1)の廃棄され
たNi−MH電池から有価物を回収する方法であり、ま
た(3)大気との接触を断つ方法が、砕断する二次電池
に水膜を形成させる方法であることを特長とする、前記
(2)の廃棄されたNi−MH電池から有価物を回収する
方法である。
[0009] (2) The method for recovering valuable resources from the discarded Ni-MH battery according to (1), wherein the crushing is performed by cutting off contact with the atmosphere. And (3) the method of cutting off contact with the atmosphere is a method of forming a water film on a secondary battery to be broken.
This is a method of recovering valuable resources from the discarded Ni-MH battery of (2).

【0010】また(4)大気との接触を断つ方法が、不
活性ガス雰囲気とする方法であることを特長とする、前
記(2)の廃棄されたNi−MH電池から有価物を回収す
る方法であり、また(5)砕断が、2軸ねじれ刃回転粉
砕機を用いた砕断であることを特長とする、前記(1)の
廃棄されたNi−MH電池から有価物を回収する方法で
あり、また(6)砕断が、低速縦型粉砕機を用いた砕断
であることを特徴とする、前記(1)の廃棄されたNi−
MH電池から有価物を回収する方法である。
(4) A method of recovering valuable materials from the discarded Ni-MH battery of (2), wherein the method of cutting off contact with the atmosphere is a method of using an inert gas atmosphere. And (5) the method of recovering valuable resources from the discarded Ni-MH battery of (1), wherein the fracturing is fracturing using a biaxial twisting blade rotary crusher. And (6) the crushing is performed by using a low-speed vertical crusher.
This is a method of recovering valuable resources from the MH battery.

【0011】また(7)砕断片が、長さが5〜20mm
の範囲の砕断片であることを特長とする、前記(1)の廃
棄されたNi−MH電池から有価物を回収する方法であ
り、また (8)砕断片を水中で処理して粉末部をスラ
リーとする方法が、砕断片に転動およびまたは超音波振
動を付与する方法であることを特長とする、前記(1)の
廃棄されたNi−MH電池から有価物を回収する方法で
ある。
(7) The crushed fragments have a length of 5 to 20 mm.
A method for recovering valuable resources from the discarded Ni-MH battery according to the above (1), characterized in that the crushed fragments are treated in water to reduce the powder portion. The method of recovering valuable resources from the discarded Ni-MH battery of the above (1), characterized in that the method of forming a slurry is a method of applying rolling and / or ultrasonic vibration to the crushed fragments.

【0012】図1は本発明の主要プロセスのフローシー
トである。図1に基づいて本発明を説明する。まず砕断
を説明する。廃棄されたMH電池は外面は合成樹脂フィ
ルムで覆われた鋼製容器でカバーされ、内部は残留水素
等によって数kg/cm2の圧力を存する場合がある。
また水素吸蔵合金は空気と接触すると一部が酸化したり
極端な場合には着火・爆発する場合がある。
FIG. 1 is a flow sheet of the main process of the present invention. The present invention will be described based on FIG. First, cutting will be described. The outer surface of the discarded MH battery is covered with a steel container covered with a synthetic resin film, and the inside may have a pressure of several kg / cm 2 due to residual hydrogen and the like.
In addition, the hydrogen storage alloy may oxidize partially when it comes into contact with air, or may ignite or explode in extreme cases.

【0013】本発明ではまずこの鋼製容器を破り内臓物
を取り出す。この際、通常のカッターを用いる切断で
は、切断部が押しつぶされて内容物を取り出し難い。従
って砕断に際しては異形ねじれ回転刃を用いることが好
ましい。例えば株式会社氏家製作所製の2軸ねじれ刃回
転粉砕機を用いて水を散布して大気とNi−MH電池と
の接触を断ちながら、Ni−MH電池を5〜20mmの
長さの砕断片に砕断したが、上述のような着火・爆発が
なく、また内容物の取り出しが容易であった。
In the present invention, the steel container is first broken to take out the internal organs. At this time, in cutting using a normal cutter, the cut portion is crushed and it is difficult to take out the contents. Therefore, it is preferable to use a deformed torsion rotary blade at the time of cutting. For example, a Ni-MH battery is cut into pieces having a length of 5 to 20 mm while spraying water using a biaxial torsion blade rotary crusher manufactured by Ujiie Seisakusho to cut off the contact between the atmosphere and the Ni-MH battery. Although crushed, there was no ignition or explosion as described above, and the contents could be easily taken out.

【0014】図2は2軸ねじれ刃回転粉砕機の例の説明
図であり、(A)は全体の説明図、(B)は異形ねじれ
回転刃の説明図である。異形ねじれ回転刃1および2は
噛み合わせて配され内転動する。この異形ねじれ回転刃
1および2が回転すると、砕断されるNi−MH電池
は、その鋼製容器部分が回転刃によって切断される。尚
異形ねじれ回転刃1および2の刃の刃幅tとピッチSを
所望のサイズとする事によって、Ni−MH電池を所望
の砕断片に砕断することができる。
FIGS. 2A and 2B are explanatory views of an example of a two-shaft twisted blade rotary crusher, wherein FIG. 2A is an overall explanatory view and FIG. 2B is an explanatory view of a deformed twisted rotary blade. The deformed torsional rotary blades 1 and 2 are arranged in mesh with each other and roll inward. When the deformed torsional rotating blades 1 and 2 rotate, the Ni-MH battery to be crushed has its steel container portion cut by the rotating blades. By setting the blade width t and the pitch S of the blades of the deformed torsional rotary blades 1 and 2 to a desired size, the Ni-MH battery can be broken into desired fragments.

【0015】また砕断するNi−MH電池を予め液体窒
素中に浸漬して低温にしておくと、Ni−MH電池の外
函である鋼製容器は低温脆性となるために砕断し易くな
る。この際は通常のロールクラッシャーやジョウクラッ
シャー等を用いてもよい。
If the Ni-MH battery to be crushed is immersed in liquid nitrogen in advance and cooled to a low temperature, the steel container, which is the outer case of the Ni-MH battery, becomes brittle at low temperature and is easily broken. . In this case, a usual roll crusher, jaw crusher, or the like may be used.

【0016】またこの砕断は、低速縦型粉砕機を用いて
行うこともできる。図3は低速縦型粉砕機の例の説明図
で、(A)はイ−イ縦断面の説明図、(B)はロ−ロ横
断面の説明図である。3は三角形のブロック状の回転刃
で、端部3−1には刃先が形成されている。5は円筒状
の壁の内面に突起して配された固定刃である。回転軸6
に取りつけられた回転刃3が回転すると、ホッパ8内に
装入されたNi−MH電池は、回転刃3の刃先3−1と
固定刃5によってNi−MH電池の鋼製容器部分が切断
される。図中4は回転軸6に取りつけられた他の回転刃
で、回転刃3と同様の作用を有する。図中7はスクリー
ンである。
This crushing can also be performed using a low-speed vertical crusher. 3A and 3B are explanatory views of an example of a low-speed vertical pulverizer, in which FIG. 3A is an explanatory view of a vertical section and FIG. 3B is an explanatory view of a horizontal cross section. Reference numeral 3 denotes a triangular block-shaped rotary blade, and a blade edge is formed at an end 3-1. Reference numeral 5 denotes a fixed blade protruding from the inner surface of the cylindrical wall. Rotary shaft 6
When the rotary blade 3 attached to the hopper 8 rotates, the steel container portion of the Ni-MH battery of the Ni-MH battery inserted into the hopper 8 is cut by the cutting edge 3-1 of the rotary blade 3 and the fixed blade 5. You. In the figure, reference numeral 4 denotes another rotary blade attached to the rotary shaft 6, which has the same function as the rotary blade 3. 7 is a screen in the figure.

【0017】本発明者等の知見によると、砕断寸法が2
0mm超では内容物が取り出し難い。しかし5mm未満
に砕断しても格別の利益はない。このため砕断片の長さ
は5〜20mmが好ましい。砕断片は水中に保管すると
よい。。
According to the knowledge of the present inventors, the breaking size is 2
If it exceeds 0 mm, it is difficult to take out the contents. However, there is no particular advantage in shredding to less than 5 mm. For this reason, the length of the crushed fragments is preferably 5 to 20 mm. The crushed pieces should be stored in water. .

【0018】砕断片は水中で処理するが、この水中処理
は、Ni−MH電池の砕断片から、内容物の粉末部をス
ラリーとして取り出すために行う。砕断した砕断片を水
中ボールミル内に装入して転動し、あるいは水に超音波
振動を付与する等の手段を施し粉末部をスラリーとして
取り出す。なおこの際バインダーや水酸化ニッケル等も
スラリーとなって取り出される。
The crushed pieces are treated in water, and the underwater treatment is performed in order to take out a powder portion of the contents as a slurry from the crushed pieces of the Ni-MH battery. The crushed pieces are placed in an underwater ball mill and rolled, or a means such as applying ultrasonic vibration to water is applied to take out the powder portion as slurry. At this time, the binder and nickel hydroxide are also taken out as a slurry.

【0019】図1の一次分離は、水中処理でスラリー化
しない部分をスラリーから分離するために行う。この分
離は、好ましくは200メッシュの篩を用い、篩下をス
ラリーとする分離が好ましい。200メッシュよりも粗
い篩では、スラリーに混入する不純物の量が多くなり回
収物の純度が低下する。本発明者等の知見では篩目が大
きい篩から順次細かい目の篩で分級し、篩上を逐次スラ
リー化しない部分として分別し、最終の篩を200メッ
シュとする事が好ましい。この方法によると、200メ
ッシュの篩の破損や損耗を大幅に防止・低減する事がで
きる。この一次分離は、液体サイクロンセパレーターあ
るいはテーブル選鉱機等を用いても行うことができる。
The primary separation in FIG. 1 is performed in order to separate a portion that does not turn into a slurry in the underwater treatment from the slurry. This separation is preferably performed by using a 200-mesh sieve and using a slurry below the sieve. With a sieve coarser than 200 mesh, the amount of impurities mixed into the slurry increases and the purity of the recovered material decreases. According to the knowledge of the present inventors, it is preferable to classify the sieve in order from a sieve having a larger sieve to a finer sieve, and to separate the sieve on the sieve as a portion which is not to be slurried successively, and to set the final sieve to 200 mesh. According to this method, breakage and wear of the 200-mesh sieve can be significantly prevented and reduced. This primary separation can also be performed using a hydrocyclone separator or a table ore separator.

【0020】一次分離で分離されたスラリー化しない部
分は、パンチングプレートやニッケル繊維や鋼製容器や
電極の端子や有機質セパレーター等の破片や合成樹脂等
で構成されている。本発明ではこのスラリー化しない部
分を、鉄鋼原料例えばフェロニッケルの原料として使用
する。フェロニッケルはニッケル鉱石と炭素と媒溶剤を
約1500℃以上に加熱・溶融して製造した、ニッケル
を約30%含有し残部が主として鉄よりなる、ステンレ
ス鋼を製造する際に用いる合金である。
The non-slurried portion separated by the primary separation is composed of a punching plate, nickel fiber, steel container, electrode terminal, debris such as an organic separator, a synthetic resin, or the like. In the present invention, the non-slurried portion is used as a raw material for steel, for example, ferronickel. Ferronickel is an alloy used for manufacturing stainless steel, which is manufactured by heating and melting nickel ore, carbon and a solvent at about 1500 ° C. or higher, containing about 30% of nickel and the balance mainly consisting of iron.

【0021】スラリー化しない部分に含有されたニッケ
ルと鉄は、フェロニッケルの製造過程でこの合金に含有
されてステンレス鋼の製造用の原料となる。スラリー化
しない部分に含有されている他の構成物はフェロニッケ
ルの製造過程で消失しあるいはスラグに含有されて廃棄
される。また一次分離で分離されたスラリー化しない部
分は、ステンレス鋼を製造する際のニッケル源として、
直接使用することもできる。
The nickel and iron contained in the non-slurried portion are contained in this alloy during the production process of ferronickel and become raw materials for producing stainless steel. Other components contained in the portion not to be slurried are lost during the production process of ferronickel or contained in slag and discarded. The non-slurried part separated by primary separation is used as a nickel source when manufacturing stainless steel,
It can also be used directly.

【0022】一次分離で分離されたスラリーは、水素吸
蔵合金と水酸化ニッケル粉とバインダー及び導電材を含
み希薄アルカリ性である。本発明ではこのスラリーを二
次分離し、水素吸蔵合金を含有する粗水素吸蔵合金部
と、水酸化ニッケルを含有する粗水酸化ニッケル部に分
別する。二次分離では、粗水素吸蔵合金部は比重が粗水
酸化ニッケル部よりも大きいために、公知の比重分離法
や浮遊分離法で分離することができる。例えば公知の水
流式テーブル選鉱機やジグ選鉱機はこの二次分離に用い
る事ができる。
The slurry separated by the primary separation contains a hydrogen storage alloy, nickel hydroxide powder, a binder and a conductive material, and is diluted alkaline. In the present invention, this slurry is secondarily separated and separated into a crude hydrogen storage alloy part containing a hydrogen storage alloy and a crude nickel hydroxide part containing nickel hydroxide. In the secondary separation, since the crude hydrogen storage alloy part has a specific gravity larger than that of the crude nickel hydroxide part, it can be separated by a known specific gravity separation method or a floating separation method. For example, a known water-flow type table ore separator or jig ore separator can be used for the secondary separation.

【0023】二次分離で得られた粗水素吸蔵合金部は、
アルコール類、ケトン類、ケロシン等の有機溶媒又は水
もしくは水に界面活性剤を加えた洗浄液で洗浄処理し、
有機質バインダー等を除去し、乾燥して精製された水素
吸蔵合金粉とする。なお乾燥に際し、80℃程度で真空
乾燥すると、水素吸蔵合金が吸蔵している水素が除去さ
れる。この精製した水素吸蔵合金粉はそのまゝ単独であ
るいは別途製造した新しい水素吸蔵合金に混合して再使
用する。また水素吸蔵合金の塊を製造する高温溶解設備
へ装入し塊状の水素吸蔵合金として再使用することもで
きる。
The crude hydrogen storage alloy obtained by the secondary separation is
Washing treatment with an organic solvent such as alcohols, ketones, kerosene or water or a washing solution obtained by adding a surfactant to water,
The organic binder and the like are removed and dried to obtain a purified hydrogen storage alloy powder. In addition, when drying in vacuum at about 80 ° C., the hydrogen occluded by the hydrogen storage alloy is removed. The purified hydrogen storage alloy powder can be reused as it is alone or mixed with a new hydrogen storage alloy manufactured separately. Further, it can be charged into a high-temperature melting facility for producing a lump of hydrogen storage alloy and reused as a lump of hydrogen storage alloy.

【0024】二次分離で得られた粗水酸化ニッケル部
は、水酸化ニッケルが主体であり、バインダー、導電材
および一部の水素吸蔵合金を含むスラリーである。これ
は洗浄濾過して必要により過剰のアルカリ液を分離後、
塩酸、硫酸、硝酸のいずれかの酸を用いてあるいはこれ
等を複合して用いて溶解し、濾過して、溶液と不溶解部
分に分別する。
The crude nickel hydroxide part obtained by the secondary separation is a slurry mainly composed of nickel hydroxide and containing a binder, a conductive material and a part of a hydrogen storage alloy. This is done by washing and filtering if necessary to separate the excess alkaline solution,
The solution is dissolved using any one of hydrochloric acid, sulfuric acid, and nitric acid, or a mixture thereof, and then filtered to separate the solution into an insoluble portion.

【0025】溶液にはニッケルイオン、少量のレアアー
スイオン、コバルトイオン、亜鉛イオン等が含有されて
いる。レアアースイオンはpHを1.5〜2.0に保ちシ
ュウ酸で処理すると沈殿物となって溶液から濾別でき
る。レアアースイオンの沈殿物を除去した溶液は、カセ
イアルカリ液で中和するとコバルト、亜鉛を含有する水
酸化ニッケルが得られる。またレアアースイオンの沈殿
物を除去した溶液を溶媒抽出するとそれぞれニッケルと
コバルトと亜鉛とを分離する事ができ、それぞれの水酸
化物や炭酸塩として回収することができる。
The solution contains nickel ions, small amounts of rare earth ions, cobalt ions, zinc ions and the like. When the rare earth ion is treated with oxalic acid while maintaining the pH at 1.5 to 2.0, it forms a precipitate and can be separated from the solution by filtration. The solution from which the precipitate of rare earth ions has been removed is neutralized with a caustic alkali solution to obtain nickel hydroxide containing cobalt and zinc. When the solution from which the rare earth ion precipitate has been removed is extracted with a solvent, nickel, cobalt, and zinc can be separated from each other, and can be recovered as the respective hydroxides and carbonates.

【0026】[0026]

【実施例1】単3タイプの廃棄されたNi−MH電池6
kgを、歯間距離5mmのグッドカッター(商品名、株
式会社氏家製作所、3馬力の2軸ねじれ刃回転粉砕機)
で、回転歯部より水をスプレーしながら砕断した。
Embodiment 1 AA type discarded Ni-MH battery 6
kg, good cutter with 5mm distance between teeth (trade name, Ujiie Seisakusho Co., Ltd., 3-horsepower 2-axis twisted blade rotary crusher)
Then, it was broken while spraying water from the rotating tooth portion.

【0027】砕断品を内容積が30リットルのステンレ
ス製のボールミル(直径30mmのステンレス製ボール
50個が内蔵されている)に移し、スプレー水と合わせ
て約15リットルの水と共に60r.p.mで1時間転動
させた。
The shredded product was transferred to a stainless steel ball mill having an internal volume of 30 liters (containing 50 stainless steel balls having a diameter of 30 mm) and sprayed together with about 15 liters of water and 60 rp. m for 1 hour.

【0028】篩目が3.0mm,0.5mm,0.075
mmの3種類の篩を、篩目が3.0mmのものを上に、
0.5mmのものを中に、0.075mmのものを下に三
段に上下に嵩ね、ボールミルの内容物を移した。更に上
部から水5リットルを加えて洗浄した。各篩の篩上(ス
ラリー化しない部分)を集め乾燥したが1.75kgで
あり、鋼の破片やニッケルの破片や合成樹脂の破片が目
視観察された。
The sieves are 3.0 mm, 0.5 mm, 0.075
mm sieve, the sieve mesh of 3.0 mm on top,
The contents of the ball mill were transferred in a three-tier manner with the 0.5 mm one inside and the 0.075 mm one below. Further, 5 liters of water was added from above to wash. The top of each sieve (the part that was not slurried) was collected and dried, but weighed 1.75 kg, and steel fragments, nickel fragments, and synthetic resin fragments were visually observed.

【0029】篩下(スラリー)はバッチ式テーブル選鉱
機を用いて水を加えながら、比重の大きい部分と比重の
小さい部分に分離した。比重の大きい部分(粗水素吸蔵
合金部)はアセトン中に分散させた後静置し、浮遊物を
含むアセトンを分離した。沈降部を真空中で40℃で乾
燥し水素吸蔵合金2.2kgが得られた。この水素吸蔵
合金は炭素含有量が0.01%、酸素含有量が0.2%で
あり、十分再使用できる品位であった。
The sieved portion (slurry) was separated into a portion having a large specific gravity and a portion having a small specific gravity while adding water using a batch type table ore separator. A portion having a large specific gravity (crude hydrogen storage alloy portion) was dispersed in acetone and then allowed to stand to separate acetone containing suspended matters. The sedimentation section was dried at 40 ° C. in a vacuum to obtain 2.2 kg of a hydrogen storage alloy. This hydrogen storage alloy had a carbon content of 0.01% and an oxygen content of 0.2%, and was of a grade that could be sufficiently reused.

【0030】上記のテーブル選鉱機で分離した比重の小
さい部分(粗水酸化ニッケル部)は、静置し、上澄液を
除去し、沈降物に35%濃度の塩酸を加え、60℃〜7
0℃に2時間加熱して反応させた。反応終了時のpHは
1.2であった。この溶液を濾過し、沈殿物を除去し、
濾液にシュウ酸を加え、pHを1.8として80℃に1
時間保持して沈殿物(レアアースのシュウ酸塩)を濾別
した。濾液に10%のカセイソーダ液を加え、水酸化ニ
ッケルを沈殿させ濾別した。この沈殿を水洗、乾燥し
て、1.8kgの水酸化ニッケルを得た。
The portion having a small specific gravity (crude nickel hydroxide portion) separated by the above table ore separator is allowed to stand, the supernatant liquid is removed, and 35% hydrochloric acid is added to the sediment.
The reaction was carried out by heating to 0 ° C. for 2 hours. The pH at the end of the reaction was 1.2. The solution was filtered to remove the precipitate,
Oxalic acid was added to the filtrate, and the pH was adjusted to 1.8 to 80 ° C.
After keeping for a time, the precipitate (rare earth oxalate) was filtered off. A 10% sodium hydroxide solution was added to the filtrate, and nickel hydroxide was precipitated and separated by filtration. The precipitate was washed with water and dried to obtain 1.8 kg of nickel hydroxide.

【0031】[0031]

【発明の効果】Ni−MH電池の廃棄物は、ニッケル、
水素吸蔵合金、バインダー、合成樹脂フィルム、鋼等
の、物理的・化学的特性が異なる多種類の部材で形成さ
れているが、本発明によると、高い価値を有する有価物
を簡易な方法で効率よく回収する事ができる。
The waste of the Ni-MH battery is nickel,
Although it is formed of various kinds of members having different physical and chemical properties, such as a hydrogen storage alloy, a binder, a synthetic resin film, and steel, according to the present invention, a valuable material having a high value can be efficiently converted by a simple method. Can be collected well.

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

【図1】は本発明の重要プロセスのフローシート。FIG. 1 is a flow sheet of an important process of the present invention.

【図2】は2軸ねじれ刃回転粉砕機の模式説明図。FIG. 2 is a schematic explanatory view of a two-axis twist blade rotary crusher.

【図3】は低速縦型粉砕機の模式説明図。FIG. 3 is a schematic explanatory view of a low-speed vertical crusher.

【符号の説明】[Explanation of symbols]

1:異形ねじれ回転刃、 2:異形ねじれ回転刃、
3:三角形のブロック状の回転刃、 4:三角形のブロ
ック状の回転刃、 5:固定刃、6:回転軸。
1: Deformed twist rotary blade 2: Deformed twist rotary blade
3: triangular block-shaped rotary blade, 4: triangular block-shaped rotary blade, 5: fixed blade, 6: rotary shaft.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 見持 洋司 茨城県つくば市東光台5−9−6 日本 重化学工業株式会社筑波研究所内 (72)発明者 本多 次徳 東京都中央区日本橋小網町8番4号 日 本重化学工業株式会社内 (56)参考文献 特開 平6−207227(JP,A) 特開 平6−340930(JP,A) (58)調査した分野(Int.Cl.6,DB名) C22B 7/00 H01M 10/54──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yoji Mizumi 5-9-6 Tokodai, Tsukuba City, Ibaraki Prefecture Japan Tsukuba Research Laboratories Co., Ltd. (72) Inventor Honda Tsugutoku Nihonbashi Koami, Chuo-ku, Tokyo No. 8-4, Nippon Heavy Industries, Ltd. (56) References JP-A-6-207227 (JP, A) JP-A-6-340930 (JP, A) (58) Fields investigated (Int. 6 , DB name) C22B 7/00 H01M 10/54

Claims (8)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】負極に粉末状水素吸蔵合金を配した、廃棄
されたニッケル−水素吸蔵合金二次電池から有価物を回
収するに際し、該二次電池を砕断し、砕断片を水中で処
理して粉末部をスラリーとし、ついでスラリー化しない
部分とスラリーとに分離し、スラリー化しない部分は鉄
鋼原料として回収し、スラリーは比重分離およびまたは
浮遊分離により粗水素吸蔵合金部と粗水酸化ニッケル部
とに分離し、粗水素吸蔵合金部は洗浄して水素吸蔵合金
として回収し、粗水酸化ニッケル部は酸溶解して不純物
を除去してニッケル化合物を回収することを特徴とす
る、廃棄されたニッケル−水素吸蔵合金二次電池から有
価物を回収する方法。
When recovering valuable resources from a discarded nickel-hydrogen storage alloy secondary battery having a powdered hydrogen storage alloy disposed on the negative electrode, the secondary battery is crushed and crushed pieces are treated in water. Then, the powder part is converted into a slurry, then the non-slurried part is separated into a slurry and the non-slurried part is recovered as a steel raw material. The slurry is separated from the crude hydrogen storage alloy part and the crude nickel hydroxide by specific gravity separation or floating separation. The crude hydrogen storage alloy part is washed and recovered as a hydrogen storage alloy, and the crude nickel hydroxide part is dissolved in acid to remove impurities and recover nickel compounds. And recovering valuable resources from the nickel-hydrogen storage alloy secondary battery.
【請求項2】砕断が、大気との接触を断って行う砕断で
あることを特徴とする、請求項1の廃棄されたニッケル
−水素吸蔵合金二次電池から有価物を回収する方法。
2. The method for recovering valuable resources from a discarded nickel-hydrogen storage alloy secondary battery according to claim 1, wherein the crushing is performed by cutting off contact with the atmosphere.
【請求項3】大気との接触を断つ方法が、砕断する二次
電池に水膜を形成させる方法であることを特長とする、
請求項2の廃棄されたニッケル−水素吸蔵合金二次電池
から有価物を回収する方法。
3. The method according to claim 1, wherein the method of cutting off the contact with the atmosphere is a method of forming a water film on a secondary battery to be broken.
A method for recovering valuable resources from the discarded nickel-hydrogen storage alloy secondary battery according to claim 2.
【請求項4】大気との接触を断つ方法が、不活性ガス雰
囲気とする方法であることを特徴とする、請求項2の廃
棄されたニッケル−水素吸蔵合金二次電池から有価物を
回収する方法。
4. A method for recovering valuable resources from a discarded nickel-hydrogen storage alloy secondary battery according to claim 2, wherein the method of cutting off contact with the atmosphere is a method of using an inert gas atmosphere. Method.
【請求項5】砕断が、2軸ねじれ刃回転粉砕機を用いた
砕断であることを特徴とする、請求項1の廃棄されたニ
ッケル−水素吸蔵合金二次電池から有価物を回収する方
法。
5. The method according to claim 1, wherein the crushing is performed using a twin-screw rotary blade rotary crusher. Method.
【請求項6】砕断が、低速縦型粉砕機を用いた砕断であ
ることを特徴とする、請求項1の廃棄されたニッケル−
水素吸蔵合金二次電池から有価物を回収する方法。
6. The scrap nickel according to claim 1, wherein the crushing is performed using a low-speed vertical crusher.
A method of recovering valuable resources from a hydrogen storage alloy secondary battery.
【請求項7】砕断片が、長さが5〜20mmの範囲の砕
断片であることを特徴とする、請求項1の廃棄されたニ
ッケル−水素吸蔵合金二次電池から有価物を回収する方
法。
7. A method for recovering valuable resources from a discarded nickel-hydrogen storage alloy secondary battery according to claim 1, wherein the fragment is a fragment having a length in the range of 5 to 20 mm. .
【請求項8】砕断片を水中で処理して粉末部をスラリー
とする方法が、砕断片に転動およびまたは超音波振動を
付与する方法であることを特徴とする、請求項1の廃棄
されたニッケル−水素吸蔵合金電池から有価物を回収す
る方法。
8. The method according to claim 1, wherein the method of treating the crushed pieces in water to turn the powder portion into a slurry is a method of applying rolling and / or ultrasonic vibration to the crushed pieces. And recovering valuable resources from the nickel-hydrogen storage alloy battery.
JP15364394A 1994-07-05 1994-07-05 Method for recovering valuable resources from discarded nickel-hydrogen storage alloy secondary batteries Expired - Lifetime JP2866005B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15364394A JP2866005B2 (en) 1994-07-05 1994-07-05 Method for recovering valuable resources from discarded nickel-hydrogen storage alloy secondary batteries

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15364394A JP2866005B2 (en) 1994-07-05 1994-07-05 Method for recovering valuable resources from discarded nickel-hydrogen storage alloy secondary batteries

Publications (2)

Publication Number Publication Date
JPH0820825A JPH0820825A (en) 1996-01-23
JP2866005B2 true JP2866005B2 (en) 1999-03-08

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ID=15567016

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JP4642952B2 (en) * 1999-06-21 2011-03-02 株式会社東芝 Method for regenerating positive electrode active material for secondary battery
JP4608773B2 (en) * 2000-12-12 2011-01-12 住友金属鉱山株式会社 Method of recovering valuable metals from used nickel metal hydride secondary batteries
JP5029858B2 (en) * 2001-07-31 2012-09-19 トヨタ自動車株式会社 Method for separating and recovering alkaline secondary battery positive electrode material, method for analyzing characteristics of alkaline secondary battery positive electrode material
FR2868603B1 (en) * 2004-04-06 2006-07-14 Recupyl Sa Sa METHOD FOR RECYCLING BATTERY MIXTURES AND BATTERIES BASED ON LITHIUM ANODE
JP5464137B2 (en) * 2010-12-14 2014-04-09 住友金属鉱山株式会社 Method for separating positive electrode active material and method for recovering valuable metal from lithium ion battery
KR101294701B1 (en) * 2012-03-28 2013-08-08 한국기초과학지원연구원 Method for manufacturing elctrode active material for secondary battery with excellent electrochemical property using ultrasound and method for manufacturing lituium secondary battery using elctrode active material manufactured by the same
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