JP7179559B2 - Apparatus and method for treating waste lithium-ion batteries - Google Patents

Apparatus and method for treating waste lithium-ion batteries Download PDF

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JP7179559B2
JP7179559B2 JP2018183335A JP2018183335A JP7179559B2 JP 7179559 B2 JP7179559 B2 JP 7179559B2 JP 2018183335 A JP2018183335 A JP 2018183335A JP 2018183335 A JP2018183335 A JP 2018183335A JP 7179559 B2 JP7179559 B2 JP 7179559B2
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resistant container
waste lithium
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JP2020049459A (en
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充志 中村
高央 市村
泰之 石田
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Taiheiyo Cement Corp
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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
    • 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

Description

本発明は、電気自動車、ハイブリッド自動車等の電源として使用された廃リチウムイオン電池の処理装置及び処理方法に関する。 TECHNICAL FIELD The present invention relates to an apparatus and method for treating waste lithium-ion batteries used as power sources for electric vehicles, hybrid vehicles, and the like.

リチウムイオン電池は、アルミ箔にリチウム、コバルト、ニッケル等を塗布した正極材と、銅箔に黒鉛等を塗布した負極材と、電解液と、セパレーター等で構成される。リチウムイオン電池は、リチウム、コバルト、ニッケル、銅、アルミニウム等の有価物を含むため、廃棄されたリチウム電池からこれらの有価物を回収することは、資源に乏しいわが国にとって極めて有益である。そこで、廃リチウムイオン電池から上記有価物を回収するため、焙焼、破砕又は粉砕、篩分け、選別等による分離回収が行われている。 A lithium-ion battery consists of a positive electrode material in which lithium, cobalt, nickel or the like is applied to an aluminum foil, a negative electrode material in which a copper foil is applied with graphite or the like, an electrolyte, a separator, and the like. Since lithium-ion batteries contain valuables such as lithium, cobalt, nickel, copper, and aluminum, recovering these valuables from discarded lithium batteries is extremely beneficial for our resource-poor country. Therefore, in order to recover the above-mentioned valuables from waste lithium ion batteries, separation and recovery by roasting, crushing or pulverization, sieving, sorting, and the like are performed.

しかし、リチウムイオン電池の電解液には、電解質となるフッ素化合物(LiPF6等)が含まれており、LiPF6は水と反応すると加水分解して有毒なフッ化水素を発生する。そこで、廃リチウムイオン電池を処理する際に、特許文献1には、揮発性のフッ素化合物(LiPF6等)等を安全に処理するため、フッ素化合物を含む電解液の揮発成分を減圧下で加熱して気化させる気化工程、気化したガスに含まれるフッ素成分をカルシウムと反応させてフッ化カルシウムとして固定するフッ素固定工程等を備えるフッ素含有電解液の処理方法が記載されている。 However, the electrolyte of a lithium ion battery contains a fluorine compound (such as LiPF 6 ) as an electrolyte, and when LiPF 6 reacts with water, it hydrolyzes to generate toxic hydrogen fluoride. Therefore, when processing waste lithium-ion batteries, in order to safely treat volatile fluorine compounds (such as LiPF 6 ), etc., in Patent Document 1, the volatile components of the electrolyte solution containing fluorine compounds are heated under reduced pressure. and a fluorine-fixing step of reacting the fluorine component contained in the vaporized gas with calcium to fix it as calcium fluoride.

一方、特許文献2には、複数個のリチウムイオン電池セルが配列された電池モジュールが箱型筺体内に複数収納されてなる電池パックを排気口が設けられた耐熱容器に格納した後、耐熱容器を熱処理炉に投入して耐熱容器をその外側からアルミニウムの融点よりも低い温度で加熱することで、耐熱容器部の電池パックを乾留して炭化混合物を分離すると共に、電池内の電解液を揮発化して耐熱容器の排気口から熱処理炉内に排出させることで、極めて簡易な作業で廃リチウムイオン電池をリサイクル処理する方法が開示されている。 On the other hand, in Patent Document 2, after storing a battery pack in which a plurality of battery modules in which a plurality of lithium ion battery cells are arranged are housed in a box-shaped housing in a heat-resistant container provided with an exhaust port, the heat-resistant container is put into a heat treatment furnace and the heat-resistant container is heated from the outside at a temperature lower than the melting point of aluminum, so that the battery pack in the heat-resistant container is dry distilled to separate the carbonized mixture, and the electrolyte in the battery is volatilized. Disclosed is a method for recycling waste lithium-ion batteries with extremely simple work by discharging the waste lithium ion batteries into a heat treatment furnace through an exhaust port of a heat-resistant container.

特開2013-229326号公報JP 2013-229326 A 特開2016-22395号公報JP 2016-22395 A

しかし、特許文献1及び特許文献2に記載の技術で加熱処理を行った後、大気下で自然冷却を行うと、加熱した廃リチウムイオン電池からはフッ化水素、塩化水素等を含む有害なガスが発生する可能性があるため安全面で課題が残る。また、自然冷却に長時間を要するため、効率的な処理の妨げになっていた。 However, after heat treatment by the techniques described in Patent Documents 1 and 2, if natural cooling is performed in the atmosphere, harmful gases containing hydrogen fluoride, hydrogen chloride, etc., are emitted from the heated waste lithium-ion batteries. There is still a safety issue because there is a possibility that In addition, the natural cooling takes a long time, which hinders efficient processing.

そこで、本発明は、上記従来の技術における問題点に鑑みてなされたものであって、安全かつ効率的に廃リチウムイオン電池を処理することを目的とする。 SUMMARY OF THE INVENTION Accordingly, the present invention has been made in view of the above-described problems in the prior art, and an object of the present invention is to treat waste lithium ion batteries safely and efficiently.

上記目的を達成するため、本発明は、廃リチウムイオン電池の処理装置であって、廃リチウムイオン電池を収容する耐熱容器と、該耐熱容器を加熱する熱処理炉と、該熱処理炉に前記耐熱容器を投入及び排出する容器搬送装置と、該容器搬送装置によって前記熱処理炉から排出された耐熱容器に冷却水を噴霧して冷却する冷却装置とを備えることを特徴とする。 In order to achieve the above object, the present invention provides an apparatus for treating waste lithium ion batteries, comprising: a heat-resistant container for containing the waste lithium-ion batteries; a heat treatment furnace for heating the heat-resistant container; and a cooling device for cooling the heat-resistant container discharged from the heat treatment furnace by the container conveying device by spraying cooling water.

本発明によれば、熱処理炉から排出された耐熱容器に冷却装置で冷却水を噴霧して熱処理後の廃リチウムイオン電池を短時間で冷却することができ、効率的に廃リチウムイオン電池を処理することができる。 According to the present invention, the heat-resistant container discharged from the heat treatment furnace can be sprayed with cooling water by the cooling device to cool the waste lithium ion batteries after the heat treatment in a short time, and the waste lithium ion batteries can be efficiently treated. can do.

上記廃リチウムイオン電池の処理装置において、前記冷却装置内が負圧になるように制御する圧力制御装置を備えることができ、これによって、フッ化水素、塩化水素等を含む有害ガスが冷却装置から放出されるのを防止することができる。 The apparatus for treating waste lithium ion batteries can be provided with a pressure control device for controlling the inside of the cooling device to have a negative pressure, whereby harmful gases including hydrogen fluoride, hydrogen chloride, etc. can be prevented from being released.

また、前記冷却装置の排ガスをセメントキルンの排ガス処理系統に供給する排ガス処理装置を備えることができ、これによって、フッ化水素、塩化水素等を含む有害ガスをセメント製造工程内のセメント原料に固定化して無害化することができる。 Further, an exhaust gas treatment device for supplying exhaust gas from the cooling device to an exhaust gas treatment system of the cement kiln can be provided, whereby harmful gases including hydrogen fluoride, hydrogen chloride, etc. are fixed to the cement raw material in the cement manufacturing process. can be rendered harmless.

さらに、本発明は、廃リチウムイオン電池の処理方法であって、廃リチウムイオン電池を収容した耐熱容器を加熱し、加熱後の耐熱容器にのみ冷却水を噴霧して冷却することを特徴とする。本発明によれば、加熱後の耐熱容器にのみ冷却水を噴霧して熱処理後の廃リチウムイオン電池を短時間で冷却することができ、効率的に廃リチウムイオン電池を処理することができる。 Furthermore, the present invention is a method for treating waste lithium-ion batteries, characterized by heating a heat-resistant container containing waste lithium-ion batteries and cooling only the heat-resistant container after heating by spraying cooling water. . According to the present invention, it is possible to cool the heat-treated waste lithium-ion batteries in a short time by spraying cooling water only on the heat-resistant container after heating, and to efficiently treat the waste lithium-ion batteries.

以上のように、本発明によれば、安全かつ効率的に廃リチウムイオン電池を処理することができる。 As described above, according to the present invention, waste lithium ion batteries can be treated safely and efficiently.

本発明に係る廃リチウムイオン電池の処理装置の一実施の形態を示す全体横断面図である。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an overall cross-sectional view showing an embodiment of a waste lithium ion battery processing apparatus according to the present invention; 本発明に係る廃リチウムイオン電池の処理装置の一実施の形態を示す全体縦断面図である。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is an overall vertical cross-sectional view showing an embodiment of a waste lithium ion battery processing apparatus according to the present invention; 図2のA矢視図であって、冷却装置及びその近傍を示す概略図である。FIG. 3 is a view in the direction of arrow A in FIG. 2 and is a schematic diagram showing a cooling device and its vicinity. 本発明に係る廃リチウムイオン電池の処理装置で用いる耐熱容器を示す縦断面図である。1 is a vertical cross-sectional view showing a heat-resistant container used in a waste lithium-ion battery processing apparatus according to the present invention. FIG. 熱処理炉に投入される直前の耐熱容器を示す横断面図である。FIG. 4 is a cross-sectional view showing the heat-resistant container just before it is put into the heat treatment furnace; 熱処理炉に投入される直前の耐熱容器を示す縦断面図である。It is a vertical cross-sectional view showing a heat-resistant container immediately before being put into a heat treatment furnace. 熱処理炉への耐熱容器の投入動作を説明するための概略図である。It is the schematic for demonstrating the injection|throwing-in operation|movement of the heat-resistant container to a heat treatment furnace. 熱処理炉への耐熱容器の投入・排出動作を説明するための概略図である。It is the schematic for demonstrating the injection|throwing-in and discharge operation|movement of the heat-resistant container to a heat treatment furnace. 熱処理炉への耐熱容器の投入・排出動作を説明するための概略図である。It is the schematic for demonstrating the injection|throwing-in and discharge operation|movement of the heat-resistant container to a heat treatment furnace. 冷却装置及び熱処理炉への耐熱容器の投入・排出動作を説明するための概略図である。It is the schematic for demonstrating the injection|throwing-in operation|movement of the heat-resistant container to a cooling device and a heat treatment furnace, and discharge|emission. 冷却装置からの耐熱容器の排出動作を説明するための概略図である。It is a schematic diagram for explaining the discharge operation of the heat-resistant container from the cooling device.

次に、本発明の一実施の形態について図面を参照しながら詳細に説明する。 An embodiment of the present invention will now be described in detail with reference to the drawings.

図1及び図2に示すように、本発明に係る廃リチウムイオン電池の処理装置1は、複数個のリチウムイオン電池セルが配列された電池モジュールが箱型筐体内に複数収納された電池パック50に加熱処理を施して有用金属を回収するものであって、主に電池パック50を格納する複数の耐熱容器2と、熱処理炉3と、熱処理炉3に耐熱容器2を投入及び排出する容器搬送装置4と、熱処理後の耐熱容器2を冷却する冷却装置31等を備える。 As shown in FIGS. 1 and 2, the waste lithium ion battery processing apparatus 1 according to the present invention includes a battery pack 50 in which a plurality of battery modules each having a plurality of lithium ion battery cells arranged therein are housed in a box-shaped housing. A plurality of heat-resistant containers 2 that mainly store battery packs 50, a heat treatment furnace 3, and a container transporter that puts the heat-resistant containers 2 into and out of the heat treatment furnace 3. A device 4 and a cooling device 31 for cooling the heat-resistant container 2 after heat treatment are provided.

耐熱容器2は、図4~図6に示すように、容器本体2Aと蓋2Bとで構成され、少なくとも650℃の耐熱温度を有する。 The heat-resistant container 2, as shown in FIGS. 4 to 6, is composed of a container body 2A and a lid 2B, and has a heat-resistant temperature of at least 650.degree.

容器本体2Aは、上方に開口して円筒状に形成された内筒2aと、内筒2aよりも大径で内筒2aを囲繞するように配置された外筒2bと、内筒2a及び外筒2bの底面に配置された複数の車輪2cと、外筒2bの周面2dに固定された2本の取っ手2eと、外筒2bの周面2dから突出するハンガー2fとで構成される。 The container main body 2A includes an inner cylinder 2a formed in a cylindrical shape with an upward opening, an outer cylinder 2b having a larger diameter than the inner cylinder 2a and arranged so as to surround the inner cylinder 2a, the inner cylinder 2a and the outer cylinder 2a. It is composed of a plurality of wheels 2c arranged on the bottom surface of the cylinder 2b, two handles 2e fixed to the peripheral surface 2d of the outer cylinder 2b, and a hanger 2f protruding from the peripheral surface 2d of the outer cylinder 2b.

一方、蓋2Bは、下方に開口する円筒状に形成された本体2nと、本体2nの周面に開口して斜め上方に突出する排気管2gと、本体2nの天井面2hに設けられた取っ手2mとで構成される。 On the other hand, the lid 2B includes a cylindrical main body 2n that opens downward, an exhaust pipe 2g that opens in the peripheral surface of the main body 2n and protrudes obliquely upward, and a handle provided on the ceiling surface 2h of the main body 2n. 2m.

図1及び図2に示すように、熱処理炉3は円筒状の縦型炉であり、4本のガスバーナー8(8A~8D)によって加熱される。ガスバーナー8の近傍にはノズル11(11A~11D)が設けられ、ファン(不図示)を介して送られる、燃焼用及び冷却用の空気Aが炉内に供給される。熱処理炉3の炉床17は、電動モータ(不図示)を備えた炉床回転装置19によって鉛直軸回りに回転し、位置決めセンサ(不図示)によって所定の位置に位置決めされる。排気管28の下流側には二次燃焼室、排気用の煙突等が設けられる As shown in FIGS. 1 and 2, the heat treatment furnace 3 is a cylindrical vertical furnace and is heated by four gas burners 8 (8A-8D). Nozzles 11 (11A to 11D) are provided near the gas burner 8, and combustion and cooling air A is supplied into the furnace via a fan (not shown). A hearth 17 of the heat treatment furnace 3 is rotated about a vertical axis by a hearth rotating device 19 equipped with an electric motor (not shown) and positioned at a predetermined position by a positioning sensor (not shown). A secondary combustion chamber, an exhaust chimney, etc. are provided downstream of the exhaust pipe 28.

熱処理炉3の炉壁7の一部には、上下に開閉式の炉体扉7bで外部と仕切られた開口部7aが形成される。開口部7aに対向する位置に、開口部7aから熱処理炉3内に耐熱容器2を投入すると共に、熱処理炉3内を一周した後の耐熱容器2を熱処理炉3から排出する容器搬送装置4が設けられる。 A part of the furnace wall 7 of the heat treatment furnace 3 is formed with an opening 7a separated from the outside by a vertically openable furnace body door 7b. At a position facing the opening 7a, a container conveying device 4 is provided for inserting the heat-resistant container 2 into the heat treatment furnace 3 from the opening 7a and for discharging the heat-resistant container 2 after going around the inside of the heat treatment furnace 3 from the heat treatment furnace 3. be provided.

容器搬送装置4は、図1、図2及び図6に示すように、熱処理炉3の開口部7aと熱処理炉3の中心を結ぶ線上の方向(図1では左右方向)に延びると共に、モーター18の正回転によって耐熱容器2に当接して耐熱容器2を熱処理炉3内に押し入れるプッシャー部4aと、耐熱容器2の容器本体2Aの外周に設けられたハンガー2fを係止する爪4cが先端に設けられ、モーター18の負回転によって耐熱容器2を熱処理炉3内から引っ張り出すプルアウト部4bを備えている。プッシャー部4aはプルアウト部4bの真上に配置される。 As shown in FIGS. 1, 2 and 6, the container conveying device 4 extends in the direction of the line connecting the opening 7a of the heat treatment furnace 3 and the center of the heat treatment furnace 3 (horizontal direction in FIG. 1). forward rotation of the heat-resistant container 2 to push the heat-resistant container 2 into the heat treatment furnace 3, and a claw 4c for locking the hanger 2f provided on the outer periphery of the container body 2A of the heat-resistant container 2. , and has a pull-out portion 4 b for pulling out the heat-resistant container 2 from the heat treatment furnace 3 by negative rotation of the motor 18 . The pusher portion 4a is arranged directly above the pullout portion 4b.

開閉式の炉体扉7bに隣接して(図1において左方)には炉前室23が設けられ、炉前室23に隣接して(図3において右方)に冷却装置31が設けられる。熱処理炉3の接線方向(図1では上下方向)に搬送装置29によって移動自在のスライドベース21が設置され、スライドベース21は、図3において、炉前室23の左方空間と、開閉式の扉24、25を隔て炉前室23及び冷却装置31の間を移動可能に構成される。 A furnace front chamber 23 is provided adjacent to the openable furnace door 7b (left side in FIG. 1), and a cooling device 31 is provided adjacent to the furnace front chamber 23 (right side in FIG. 3). . A slide base 21 is installed in the tangential direction of the heat treatment furnace 3 (vertical direction in FIG. 1) and is movable by a conveying device 29. The slide base 21, in FIG. It is configured to be movable between the furnace front chamber 23 and the cooling device 31 with the doors 24 and 25 separated.

冷却装置31は、開閉式の扉25を隔てて炉前室23に隣接し、内部には、熱処理炉3から排出された耐熱容器2に冷却水を噴霧するための噴霧装置31a~31cを備える。噴霧装置31aは耐熱容器2の天井部に冷却水を噴霧し、噴霧装置31b、31cは耐熱容器2の側面に冷却水を噴霧する。また、噴霧した後の水を回収するための排水口31dが冷却装置31の底面に穿設される。 The cooling device 31 is adjacent to the furnace front chamber 23 across an openable door 25, and includes spray devices 31a to 31c for spraying cooling water to the heat-resistant container 2 discharged from the heat treatment furnace 3. . The spray device 31 a sprays cooling water onto the ceiling of the heat-resistant container 2 , and the spray devices 31 b and 31 c spray cooling water onto the sides of the heat-resistant container 2 . Also, a drain port 31d is formed in the bottom surface of the cooling device 31 for collecting water after spraying.

また、冷却装置31の内部が負圧になるように制御する圧力制御装置が設けられ、圧力制御装置は、冷却装置31の内部の圧力を測定する圧力計と、冷却装置31の排ガスを吸引する吸引装置と、前記圧力計の測定値が負圧になるように吸引装置を制御するコントローラ等を備える。さらに、冷却装置31の排ガスをセメントキルンの排ガス処理系統に供給する排ガス処理装置(不図示)が設けられる。 In addition, a pressure control device is provided to control the inside of the cooling device 31 to have a negative pressure. A suction device and a controller or the like for controlling the suction device so that the measured value of the pressure gauge becomes a negative pressure are provided. Further, an exhaust gas treatment device (not shown) is provided for supplying the exhaust gas from the cooling device 31 to an exhaust gas treatment system of the cement kiln.

次に、上記構成を有する廃リチウムイオン電池の処理装置1を用いた廃リチウムイオン電池の処理方法について説明する。尚、以下の説明では、処理装置1によってハイブリッド自動車や電気自動車等から取外されたままの電池パック50を処理する場合を例示する。 Next, a method for processing waste lithium ion batteries using the waste lithium ion battery processing apparatus 1 having the above configuration will be described. In the following description, a case where the processing device 1 processes the battery pack 50 that has been removed from a hybrid vehicle, an electric vehicle, or the like will be exemplified.

熱処理炉3の内部の温度を650℃に昇温し、クレーン等(不図示)を使用して、図7に示すように、電池パック50を格納した耐熱容器2Nをスライドベース21の右端部に載置する。扉24を開放した後、搬送装置29を介してスライドベース21を右方に移動させ、耐熱容器2を炉体扉7bの正面まで移動させた後、扉24を閉じて炉体扉7bを開放し、容器搬送装置4のプッシャー部4aを前進させて耐熱容器2Nを熱処理炉3内に投入する。これにより、耐熱容器2Nは熱処理炉3の炉床17上、図1では9時の位置に載置される。 The temperature inside the heat treatment furnace 3 is raised to 650° C., and a crane or the like (not shown) is used to move the heat-resistant container 2N containing the battery pack 50 to the right end of the slide base 21 as shown in FIG. Place. After opening the door 24, the slide base 21 is moved to the right via the transfer device 29, the heat-resistant container 2 is moved to the front of the furnace door 7b, and then the door 24 is closed to open the furnace door 7b. Then, the pusher portion 4a of the container conveying device 4 is advanced to load the heat-resistant container 2N into the heat treatment furnace 3. As shown in FIG. As a result, the heat-resistant container 2N is placed on the hearth 17 of the heat treatment furnace 3, at the 9 o'clock position in FIG.

容器搬送装置4のプッシャー部4aを後退させた後、炉体扉7bを閉鎖し、炉床回転装置19を介して炉床17を45゜左回転させる。この45゜の回転は、特に限定されるものではないが、例えば、37.5分毎に炉床17を45゜ずつ回転させることで、5時間で炉床17が1回転するように設定している。 After retracting the pusher portion 4a of the container transfer device 4, the furnace door 7b is closed, and the hearth 17 is rotated counterclockwise by 45° via the hearth rotating device 19. As shown in FIG. This 45° rotation is not particularly limited, but for example, the hearth 17 is set to rotate once every 5 hours by rotating the hearth 17 by 45° every 37.5 minutes. ing.

上記動作を7回繰り返すことで、熱処理炉3の炉床17上には、図1に示したように、隣接する耐熱容器2が一定の間隔を開けた状態で8個の耐熱容器2が環状に載置される。 By repeating the above operation seven times, on the hearth 17 of the heat treatment furnace 3, as shown in FIG. is placed on

上記動作の間、耐熱容器2は熱処理炉3内で1周する間に外側から加熱されることで、耐熱容器2内は還元雰囲気となり、耐熱容器2に格納された電池パック50の樹脂製の筐体等のプラスチック類は乾留により炭化混合物としてリチウム、コバルト、ニッケル、マンガン等の有用金属が含まれた材料から分離された状態となっている。尚、耐熱容器2はアルミニウムの融点(660℃)よりも低い温度(650℃)で加熱されるので電池パック50内で使用されたアルミニウム成分が溶け出すことはない。また、電池内の電解液は揮発し、プラスチック等の可燃性物質が熱分解することによって発生したガスと共に、耐熱容器2の排気管2gから熱処理炉3内に排出される。熱処理炉3内の未燃焼ガスは二次燃焼室に導かれ、熱処理炉3の温度(650℃)よりも高い温度(800℃)で燃焼する。 During the above operation, the heat-resistant container 2 is heated from the outside while making one revolution in the heat treatment furnace 3, so that the inside of the heat-resistant container 2 becomes a reducing atmosphere, and the battery pack 50 stored in the heat-resistant container 2 is made of resin. Plastics such as the housing are in a state of being separated from materials containing useful metals such as lithium, cobalt, nickel and manganese as a carbonized mixture by dry distillation. Since the heat-resistant container 2 is heated at a temperature (650° C.) lower than the melting point (660° C.) of aluminum, the aluminum component used in the battery pack 50 does not melt. Further, the electrolyte in the battery volatilizes and is discharged into the heat treatment furnace 3 through the exhaust pipe 2g of the heat-resistant container 2 together with gas generated by thermal decomposition of combustible substances such as plastics. The unburned gas in the heat treatment furnace 3 is led to the secondary combustion chamber and burned at a temperature (800° C.) higher than the temperature of the heat treatment furnace 3 (650° C.).

耐熱容器2が熱処理炉3内で1周する前に、図8に示すように、電池パック50を格納した新たな耐熱容器2Nを左端部に載置したスライドベース21の右半分を炉前室23に挿入する。この際、扉24は閉じられている。 Before the heat-resistant container 2 makes one turn in the heat treatment furnace 3, as shown in FIG. 23. At this time, the door 24 is closed.

耐熱容器2が熱処理炉3内で1周すると、炉体扉7bを開放して容器搬送装置4のプルアウト部4bを耐熱容器2の位置まで前進させ、図6に示すように、プルアウト部4b先端に設けられた爪4cを、耐熱容器2に設けられたハンガー2fに係止させる。そして、プルアウト部4bを後退させ、図9に示すように、熱処理後の耐熱容器2Tを熱処理炉3から引き出してスライドベース21上に載置し、炉体扉7bを閉鎖する。 When the heat-resistant container 2 makes one turn in the heat treatment furnace 3, the furnace door 7b is opened to advance the pull-out portion 4b of the container transfer device 4 to the position of the heat-resistant container 2, and as shown in FIG. A hook 4c provided on the heat-resistant container 2 is engaged with a hanger 2f provided on the heat-resistant container 2. As shown in FIG. Then, the pull-out portion 4b is retracted, and as shown in FIG. 9, the heat-resistant container 2T after heat treatment is pulled out from the heat treatment furnace 3 and placed on the slide base 21, and the furnace body door 7b is closed.

次に、扉24、25を開放した後、スライドベース21を右方に移動し、電池パック50を格納した新たな耐熱容器2Nを炉体扉7bの正面まで移動させると共に、熱処理済みの耐熱容器2Tを冷却装置31に移動させて扉24、25を閉じる。この状態を図10に示す。 Next, after the doors 24 and 25 are opened, the slide base 21 is moved to the right to move the new heat-resistant container 2N containing the battery pack 50 to the front of the furnace door 7b. 2T is moved to the cooling device 31 and the doors 24 and 25 are closed. This state is shown in FIG.

図10の状態から、新たな耐熱容器2Nを上述の要領で熱処理炉3内に投入して加熱すると共に、熱処理済みの耐熱容器2Tを冷却装置31で冷却する。冷却装置31において、噴霧装置31aによって耐熱容器2Tの天井部に冷却水を噴霧し、噴霧装置31b、31cによって耐熱容器2Tの側面に冷却水を噴霧する。噴霧した後の水は、排水口31dから回収する。従来の自然冷却では650℃程度まで加熱した電池パック50を150℃程度まで冷却するのに6時間程度を要したが、この冷却水の噴霧による冷却により、1時間程度、すなわち従来の1/6程度で冷却工程が完了する。また、電池パック重量や加熱温度が変化した場合でも、水の噴霧量を調整することで冷却工程を短縮することが可能である。 From the state of FIG. 10, a new heat-resistant container 2N is put into the heat treatment furnace 3 in the manner described above and heated, and the heat-treated heat-resistant container 2T is cooled by the cooling device 31. In the cooling device 31, the spray device 31a sprays cooling water onto the ceiling of the heat-resistant container 2T, and the spray devices 31b and 31c spray cooling water onto the side surfaces of the heat-resistant container 2T. The water after spraying is recovered from the drain port 31d. With conventional natural cooling, it takes about 6 hours to cool the battery pack 50 heated to about 650° C. to about 150° C., but with cooling by this cooling water spray, it takes about 1 hour, that is, one-sixth of the conventional cooling time. The cooling process is completed in about. Moreover, even if the battery pack weight or the heating temperature changes, the cooling process can be shortened by adjusting the amount of sprayed water.

次に、扉24、25を開放した後、冷却済みの耐熱容器2Cが載置されたスライドベース21を左方に移動させ、クレーン等で次工程へ搬送する。 Next, after opening the doors 24 and 25, the slide base 21 on which the cooled heat-resistant container 2C is placed is moved to the left and conveyed to the next process by a crane or the like.

冷却後の加熱処理済みの耐熱容器2Cは、内部の電池パック50を破砕、分級して炭化混合物を取り除いた後、リチウム、コバルト、ニッケル、マンガン等の有用金属をさらに分離する処理が行われる。また、電池パック50の破砕物を磁選機にかけて、鉄筐体、ねじ等の磁着物と、銅とアルミニウムからなるミックメタルに分離し、ミックメタルを比重選別してアルミ塊及び銅塊と、銅箔及びアルミ箔の積層物とに分けた後、選別機でさらに銅箔とアルミ箔とに分けることができる。 In the heat-treated heat-resistant container 2C after cooling, the battery pack 50 inside is crushed and classified to remove the carbonized mixture, and then useful metals such as lithium, cobalt, nickel, and manganese are further separated. Further, the crushed material of the battery pack 50 is subjected to a magnetic separator to separate magnetic substances such as iron casings and screws from Mik-Metal consisting of copper and aluminum. After separating into foil and aluminum foil laminate, it can be further separated into copper foil and aluminum foil by a sorter.

また、冷却装置31からのフッ化水素、塩化水素等を含む有害ガスは、排ガス処理装置によってセメントキルンの排ガス処理系統に供給し、セメント製造工程内のセメント原料に固定化して無害化する。 Harmful gases containing hydrogen fluoride, hydrogen chloride, etc. from the cooling device 31 are supplied to the exhaust gas treatment system of the cement kiln by the exhaust gas treatment device, and are fixed in cement raw materials in the cement manufacturing process to render them harmless.

尚、熱処理炉3は、炉床17が回転するものでなくてもよく、バッチ式のものでも適用可能である。また、熱源として電気や重油を使用した各種炉を使用することもでき、既存の製造設備、例えば、セメント焼成装置からの排ガスを熱源として用いてもよい。 The heat treatment furnace 3 does not have to have a rotating hearth 17, and a batch type furnace is also applicable. Various furnaces using electricity or heavy oil can also be used as heat sources, and exhaust gas from existing manufacturing facilities, for example, cement baking equipment, can be used as heat sources.

また、本実施の形態では、電池パック50を電池セルを個々に取外すことなくそのままの状態のものに対して加熱処理したが、電池パック50から分解した電池モジュール単位のものや、電池セルを個々に取外したものを格納した耐熱容器2を熱処理炉3に投入して加熱処理してもよい。 In the present embodiment, the battery pack 50 is heat-treated as it is without removing the battery cells individually. The heat-resistant container 2 containing the removed items may be placed in the heat treatment furnace 3 for heat treatment.

1 廃リチウムイオン電池の処理装置
2 耐熱容器
3 熱処理炉
4 容器搬送装置
7 炉壁
8(8A~8D) ガスバーナー
11(11A~11D) ノズル
17 炉床
18 モーター
19 炉床回転装置
21 スライドベース
23 炉前室
24、25 扉
29 搬送装置
31 冷却装置
50 電池パック
1 waste lithium ion battery processing device 2 heat-resistant container 3 heat treatment furnace 4 container transport device 7 furnace wall 8 (8A to 8D) gas burner 11 (11A to 11D) nozzle 17 hearth 18 motor 19 hearth rotating device 21 slide base 23 Front chambers 24, 25 Door 29 Transfer device 31 Cooling device 50 Battery pack

Claims (4)

廃リチウムイオン電池を収容する耐熱容器と、
該耐熱容器を加熱する熱処理炉と、
該熱処理炉に前記耐熱容器を投入及び排出する容器搬送装置と、
該容器搬送装置によって前記熱処理炉から排出された耐熱容器に冷却水を噴霧して冷却する冷却装置とを備えることを特徴とする廃リチウムイオン電池の処理装置。
a heat-resistant container for housing waste lithium-ion batteries;
a heat treatment furnace for heating the heat-resistant container;
a container conveying device for loading and unloading the heat-resistant container into and from the heat treatment furnace;
and a cooling device for cooling the heat-resistant container discharged from the heat treatment furnace by the container conveying device by spraying cooling water.
前記冷却装置内が負圧になるように制御する圧力制御装置を備えることを特徴とする請求項1に記載の廃リチウムイオン電池の処理装置。 2. The apparatus for treating waste lithium ion batteries according to claim 1, further comprising a pressure control device for controlling the inside of said cooling device to have a negative pressure. 前記冷却装置の排ガスをセメントキルンの排ガス処理系統に供給する排ガス処理装置を備えることを特徴とする請求項1又は2に記載の廃リチウムイオン電池の処理装置。 3. The apparatus for treating waste lithium ion batteries according to claim 1, further comprising an exhaust gas treatment device for supplying exhaust gas from said cooling device to an exhaust gas treatment system of a cement kiln. 廃リチウムイオン電池を収容した耐熱容器を加熱し、
加熱後の耐熱容器にのみ冷却水を噴霧して冷却することを特徴とする廃リチウムイオン電池の処理方法。
Heat the heat-resistant container containing the waste lithium-ion battery,
A method for treating waste lithium-ion batteries, comprising spraying cooling water only on the heat-resistant container after heating to cool the container.
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