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JP2011082059A - Electrode drying device and electrode drying method - Google Patents

Electrode drying device and electrode drying method Download PDF

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JP2011082059A
JP2011082059A JP2009234321A JP2009234321A JP2011082059A JP 2011082059 A JP2011082059 A JP 2011082059A JP 2009234321 A JP2009234321 A JP 2009234321A JP 2009234321 A JP2009234321 A JP 2009234321A JP 2011082059 A JP2011082059 A JP 2011082059A
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induction heating
electrode
cooling
solvent
electrode drying
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JP5503937B2 (en
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Shigenori Kazama
重徳 風間
Jiro Kishitani
二郎 岸谷
Takeshi Matsuyama
剛 松山
Masahito Shirakata
雅人 白方
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Nissan Motor Co Ltd
Envision AESC Energy Devices Ltd
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Nissan Motor Co Ltd
NEC Energy Devices 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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    • Y02E60/10Energy storage using batteries

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Abstract

【課題】凝結した溶剤が乾燥した電極膜へ再付着することを防ぎ、均一に乾燥した電極膜を作製することができる電極乾燥装置を提供する。
【解決手段】誘導加熱によって電極箔7を乾燥させる電極乾燥装置であって、電極箔7を誘導加熱によって加熱する誘導加熱手段3と、誘導加熱手段3によって電極箔7から蒸発した溶剤蒸気を凝結させる冷却手段41(42)と、冷却手段41(42)によって凝結した溶剤を回収する回収手段43と、誘導加熱手段3、冷却手段41(42)、及び回収手段43を格納する電極乾燥室2と、を備える。
【選択図】図1
An electrode drying apparatus capable of preventing a condensed solvent from re-adhering to a dried electrode film and producing a uniformly dried electrode film.
An electrode drying apparatus for drying an electrode foil by induction heating, the induction heating means for heating the electrode foil by induction heating, and a solvent vapor evaporated from the electrode foil by the induction heating means. The cooling means 41 (42) to be recovered, the recovery means 43 to recover the solvent condensed by the cooling means 41 (42), the induction heating means 3, the cooling means 41 (42), and the electrode drying chamber 2 storing the recovery means 43 And comprising.
[Selection] Figure 1

Description

本発明は、誘導加熱によって、活物質が塗布された電極を乾燥させる技術に関する。 The present invention relates to a technique for drying an electrode coated with an active material by induction heating.

従来、リチウム電池等の電池用電極膜の製造において、電極膜を乾燥させるために、誘導加熱によって電極膜を乾燥させる誘導加熱方式が知られている(例えば、特許文献1参照)。特許文献1に記載された技術によると、誘導加熱コイルの磁束を磁気コアによって集電体に集中させて、集電体を発熱させることができる。これによって、集電体の表面に塗布された活物質を乾燥させることができる。   Conventionally, in the production of an electrode film for a battery such as a lithium battery, an induction heating method is known in which the electrode film is dried by induction heating in order to dry the electrode film (see, for example, Patent Document 1). According to the technique described in Patent Document 1, the current collector can be heated by concentrating the magnetic flux of the induction heating coil on the current collector by the magnetic core. Thereby, the active material applied to the surface of the current collector can be dried.

特開2004−327203号公報JP 2004-327203 A 特開平9−283123号公報JP-A-9-283123

前述した特許文献1に記載された誘導加熱コイル(及び磁気コア)等を用いる従来の誘導加熱方式では、誘導加熱コイルの温度上昇を防ぐために、例えば、誘導加熱コイルの内部に備えられた冷却水路に冷却液を供給することによって、誘導加熱コイル自体を冷却している。このため、発生した溶剤蒸気が乾燥炉内で凝結することがある。これによって、乾燥炉の天井部又は誘導加熱コイルの周囲で凝結した溶剤が落下し、落下した溶剤が乾燥した電極膜に再付着する可能性がある。   In the conventional induction heating method using the induction heating coil (and magnetic core) described in Patent Document 1 described above, for example, a cooling water channel provided inside the induction heating coil in order to prevent a temperature rise of the induction heating coil. The induction heating coil itself is cooled by supplying a cooling liquid to. For this reason, the generated solvent vapor may condense in the drying furnace. As a result, the solvent condensed around the ceiling of the drying furnace or around the induction heating coil may fall, and the dropped solvent may be reattached to the dried electrode film.

つまり、特許文献1に記載された技術では、乾燥炉内で凝結した溶剤の処理について考慮されておらず、均一に乾燥した電極膜を作製することが難しいという問題があった。   That is, the technique described in Patent Document 1 does not consider the treatment of the solvent condensed in the drying furnace, and has a problem that it is difficult to produce a uniformly dried electrode film.

本発明は前述した問題に鑑みてなされたものであって、発生した溶剤蒸気を冷却によって積極的に凝結させ、凝結した溶剤が乾燥した電極膜へ再付着することを防ぎ、均一に乾燥した電極膜を作製することができる技術を提供することを目的とする。   The present invention has been made in view of the above-mentioned problems, and the generated solvent vapor is actively condensed by cooling, preventing the condensed solvent from reattaching to the dried electrode film, and uniformly drying the electrode. An object is to provide a technique capable of manufacturing a film.

本発明は、誘導加熱によって電極箔を乾燥させる電極乾燥装置である。この電極乾燥装置は、電極箔を誘導加熱によって加熱する誘導加熱手段と、前記誘導加熱手段によって前記電極箔から蒸発した溶剤蒸気を凝結させる冷却手段と、前記冷却手段によって凝結した溶剤を回収する回収手段と、前記誘導加熱手段、前記冷却手段、及び前記回収手段を格納する電極乾燥室と、を備えることを特徴とする。   The present invention is an electrode drying apparatus for drying an electrode foil by induction heating. The electrode drying apparatus includes an induction heating unit that heats the electrode foil by induction heating, a cooling unit that condenses the solvent vapor evaporated from the electrode foil by the induction heating unit, and a recovery that collects the solvent condensed by the cooling unit. And an electrode drying chamber for storing the induction heating means, the cooling means, and the recovery means.

また、電極乾燥室内において、活物質が塗布された電極箔を乾燥させる電極乾燥方法である。この電極乾燥方法は、誘導加熱によって前記電極箔を加熱し、前記加熱された電極箔から蒸発した溶剤蒸気を冷却することによって凝結させ、前記凝結した溶剤を回収することを特徴とする。   Further, the electrode drying method is for drying an electrode foil coated with an active material in an electrode drying chamber. This electrode drying method is characterized in that the electrode foil is heated by induction heating, the solvent vapor evaporated from the heated electrode foil is cooled to condense, and the condensed solvent is recovered.

本発明によれば、電極箔から蒸発した溶剤蒸気を冷却して凝結させ、凝結した溶剤を回収するので、凝結した溶剤が電極に再付着することを防ぐことができる。   According to the present invention, the solvent vapor evaporated from the electrode foil is cooled and condensed, and the condensed solvent is recovered. Therefore, the condensed solvent can be prevented from reattaching to the electrode.

本発明の第1の実施形態の電極乾燥装置の構成を示す説明図である。It is explanatory drawing which shows the structure of the electrode drying apparatus of the 1st Embodiment of this invention. 本発明の第1の実施形態の冷却装置の構成を示す説明図である。It is explanatory drawing which shows the structure of the cooling device of the 1st Embodiment of this invention. 本発明の第1の実施形態の誘導加熱装置の配置の例を示す説明図である。It is explanatory drawing which shows the example of arrangement | positioning of the induction heating apparatus of the 1st Embodiment of this invention. 本発明の第1の実施形態の冷却装置の配置の例を示す説明図である。It is explanatory drawing which shows the example of arrangement | positioning of the cooling device of the 1st Embodiment of this invention. 本発明の第2の実施形態の冷却装置の配置の例を示す説明図である。It is explanatory drawing which shows the example of arrangement | positioning of the cooling device of the 2nd Embodiment of this invention. 本発明の第3の実施形態の冷却装置の構成を示す説明図である。It is explanatory drawing which shows the structure of the cooling device of the 3rd Embodiment of this invention.

以下、本発明の実施形態について、図面を用いて説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

[実施形態1]
図1は、本発明の第1の実施形態の電極乾燥装置の構成を示す説明図である。
[Embodiment 1]
FIG. 1 is an explanatory diagram showing the configuration of the electrode drying apparatus according to the first embodiment of the present invention.

本実施形態の電極乾燥装置は、電極製造装置において、電極用の活物質が塗布された集電体7を誘導加熱によって乾燥させる装置であり、誘導加熱装置3、冷却装置4、及び誘導加熱装置3と冷却装置4とを格納する誘導加熱乾燥炉2、を備える。   The electrode drying apparatus of the present embodiment is an apparatus for drying the current collector 7 coated with the electrode active material by induction heating in the electrode manufacturing apparatus. The induction heating apparatus 3, the cooling apparatus 4, and the induction heating apparatus. 3 and the induction heating drying furnace 2 which stores the cooling device 4 is provided.

なお、電極製造装置は、電極乾燥装置の他、例えば、塗工機1、及び移送装置8を備える。   In addition, an electrode manufacturing apparatus is provided with the coating machine 1 and the transfer apparatus 8 other than an electrode drying apparatus, for example.

塗工機1は、活物質を帯状の集電体7に塗布する。塗工機については、広く知られた技術であるので、詳細な説明については省略する。   The coating machine 1 applies the active material to the strip-shaped current collector 7. Since the coating machine is a well-known technique, a detailed description thereof will be omitted.

活物質は、正極又は負極の活物質、導電材及び結着剤を有機溶剤に分散することによって調製される。なお、活物質は、電池の種類に応じて適宜選択される。例えば、リチウム電池の正極に用いられる活物質には、LiMn24等のリチウム及び遷移金属の複合酸化物がある。また、例えば、リチウム電池の負極に用いられる活物質には、黒鉛、金属リチウム、リチウム合金、スズ化合物等の金属材料、導電性ポリマー等がある。 The active material is prepared by dispersing the positive or negative electrode active material, the conductive material, and the binder in an organic solvent. The active material is appropriately selected according to the type of battery. For example, an active material used for a positive electrode of a lithium battery includes a composite oxide of lithium and a transition metal such as LiMn 2 O 4 . Further, for example, active materials used for the negative electrode of a lithium battery include metal materials such as graphite, metallic lithium, lithium alloy, and tin compounds, conductive polymers, and the like.

また、導電剤とは、正極の導電性を確保するために用いられる物質であり、例えば、カーボンブラック、アセチレンブラック等である。また、結着剤とは、活物質の粒子をつなぎ止める作用を持つ化合物であり、例えば、ポリフッ化ビニリデン(PVDF)、ポリ塩化ビニリデン、ポリテトラフルオロエチレン(PTFE)等である。   Further, the conductive agent is a substance used for ensuring the conductivity of the positive electrode, such as carbon black and acetylene black. In addition, the binder is a compound having an action of holding active material particles together, and examples thereof include polyvinylidene fluoride (PVDF), polyvinylidene chloride, and polytetrafluoroethylene (PTFE).

集電体7は、電池の種類に応じて適宜選択される帯状の電極箔であり、正極の場合、例えば、アルミニウム、ステンレス等であり、負極の場合、銅、ニッケル等である。   The current collector 7 is a strip-shaped electrode foil that is appropriately selected according to the type of battery. In the case of the positive electrode, for example, aluminum and stainless steel are used, and in the case of the negative electrode, copper, nickel, and the like are used.

誘導加熱装置3は、誘導加熱によって、活物質が塗布された集電体7を加熱する。誘導加熱装置3の構成については、図3を用いて後述する。   The induction heating device 3 heats the current collector 7 coated with the active material by induction heating. The configuration of the induction heating device 3 will be described later with reference to FIG.

冷却装置4は、誘導加熱によって蒸発した溶剤蒸気を冷却することによって、溶剤蒸気を凝結させ、凝結した溶剤を回収する。冷却装置4の構成の詳細については、図2を用いて後述する。   The cooling device 4 condenses the solvent vapor by cooling the solvent vapor evaporated by induction heating, and collects the condensed solvent. Details of the configuration of the cooling device 4 will be described later with reference to FIG.

移送装置8は、集電体7を略水平状態に保持し、保持された集電体7を誘導加熱乾燥炉2に連続的に送り出す。   The transfer device 8 holds the current collector 7 in a substantially horizontal state, and continuously sends the held current collector 7 to the induction heating drying furnace 2.

図2は、本発明の第1の実施形態の冷却装置4の構成を示す説明図である。   FIG. 2 is an explanatory diagram showing the configuration of the cooling device 4 according to the first embodiment of the present invention.

冷却装置4は、冷却板41、回収桶43、ダクト44及びファン45を備える。なお、冷却板41の構成は特に制限されない。例えば、冷却板41は、銅、銅合金等が鍛造又は圧延されたインゴットで構成され、内部に冷却水(冷却媒体)の通路を備え、冷却水(冷却媒体)を供給又は排出するための連結管に接続される。   The cooling device 4 includes a cooling plate 41, a recovery rod 43, a duct 44 and a fan 45. The configuration of the cooling plate 41 is not particularly limited. For example, the cooling plate 41 is composed of an ingot formed by forging or rolling copper, a copper alloy, or the like, and has a passage for cooling water (cooling medium) inside, and is connected to supply or discharge the cooling water (cooling medium). Connected to the tube.

溶剤蒸気は、ファン45によって、ダクト44の吸い込み口46から吸引され、冷却板41によって冷却される。溶剤蒸気は、冷却されると凝結し、凝結した溶剤は、冷却板41の内壁に付着する。   The solvent vapor is sucked from the suction port 46 of the duct 44 by the fan 45 and cooled by the cooling plate 41. The solvent vapor condenses when cooled, and the condensed solvent adheres to the inner wall of the cooling plate 41.

そして、付着した溶剤は、冷却板41の内壁に沿って落下し、回収桶43によって回収される。また、溶剤蒸気は、冷却板41を通過すると乾燥空気となり、ファン45によって、ダクト44から排出される。   Then, the adhering solvent falls along the inner wall of the cooling plate 41 and is recovered by the recovery rod 43. Further, the solvent vapor becomes dry air when passing through the cooling plate 41 and is discharged from the duct 44 by the fan 45.

なお、誘導加熱方式では、誘導加熱乾燥炉2の内部に熱風を還流させる必要がない。また、有機溶剤の沸点は一般的に低い(例えば、30°Cから45°C)。このため、冷却装置4は、溶剤蒸気を室温よりもわずかに高い温度まで冷却するだけで、溶剤蒸気から溶剤を除去することできる。したがって、本実施形態の電極乾燥装置は、冷却装置4を運転するコストを低減させることができる。   In the induction heating method, it is not necessary to recirculate hot air into the induction heating drying furnace 2. Moreover, the boiling point of the organic solvent is generally low (for example, 30 ° C to 45 ° C). For this reason, the cooling device 4 can remove the solvent from the solvent vapor only by cooling the solvent vapor to a temperature slightly higher than room temperature. Therefore, the electrode drying apparatus of this embodiment can reduce the cost of operating the cooling device 4.

図3は、本発明の第1の実施形態の誘導加熱装置3の配置の例を示す説明図である。   Drawing 3 is an explanatory view showing an example of arrangement of induction heating device 3 of a 1st embodiment of the present invention.

誘導加熱装置3は、例えば、電力を供給する電源33、誘導電流を発生させる共振周波数自動調整器34、誘導電流を制御するトランス35、誘導加熱コイル31及び磁束を集中させる磁気コア32を備える。   The induction heating device 3 includes, for example, a power supply 33 that supplies electric power, a resonance frequency automatic regulator 34 that generates an induction current, a transformer 35 that controls the induction current, an induction heating coil 31, and a magnetic core 32 that concentrates magnetic flux.

誘導加熱コイル31は、例えば、直線部36を持つ略矩形状の一重又は多重の扁平コイルである。略矩形状の直線部36は、帯状の集電体7の幅方向に沿って配置される。誘導加熱コイル31は、誘導電流によって、磁束を発生させる。   The induction heating coil 31 is, for example, a substantially rectangular single or multiple flat coil having a straight portion 36. The substantially rectangular straight portion 36 is arranged along the width direction of the belt-like current collector 7. The induction heating coil 31 generates a magnetic flux by an induced current.

磁気コア32は、例えば、凹部の形状のフェライトであり、帯状の集電体7の幅方向に沿って配置される誘導加熱コイル31の直線部36を収容する。磁気コア32は、誘導加熱コイル31が発生させた磁束を集中させる。磁気コアによって集中された磁束は、集電体7を透過する。集電体7は、この磁束によって発熱する。   The magnetic core 32 is, for example, a ferrite in the shape of a recess, and accommodates the linear portion 36 of the induction heating coil 31 disposed along the width direction of the belt-like current collector 7. The magnetic core 32 concentrates the magnetic flux generated by the induction heating coil 31. The magnetic flux concentrated by the magnetic core passes through the current collector 7. The current collector 7 generates heat due to this magnetic flux.

電源33は、入力された交流電流を直流電流として供給する装置である。共振周波数自動調整器34は、電源33から供給された直流電流を交流電流に変換し、変換された交流電流の周波数を制御することによって、誘導電流を発生させる。トランス35は、電圧を増減させることによって、誘導加熱コイル31に供給される誘導電流の大きさを制御する。なお、誘導加熱装置3は、広く知られた技術であるので、各構成の詳細な説明については省略する。   The power source 33 is a device that supplies an input alternating current as a direct current. The automatic resonance frequency adjuster 34 converts the direct current supplied from the power supply 33 into an alternating current, and generates an induced current by controlling the frequency of the converted alternating current. The transformer 35 controls the magnitude of the induction current supplied to the induction heating coil 31 by increasing or decreasing the voltage. In addition, since the induction heating apparatus 3 is a well-known technique, detailed description of each structure is abbreviate | omitted.

図4は、本発明の第1の実施形態の冷却装置4の配置の例を示す説明図である。   FIG. 4 is an explanatory diagram showing an example of the arrangement of the cooling device 4 according to the first embodiment of the present invention.

図4では、一組の誘導加熱装置3及び一つの冷却装置4が図示されている。   In FIG. 4, a set of induction heating devices 3 and a cooling device 4 are shown.

図4に示す点線で囲まれた部分は、図3に示した誘導加熱装置3の一部であり、集電体7の上下に配置された一組の誘導加熱コイル31及び磁気コア32を、集電体の長さ方向に沿って切り取った断面(図3のA−Aの断面)である。   A part surrounded by a dotted line shown in FIG. 4 is a part of the induction heating device 3 shown in FIG. 3, and a set of induction heating coils 31 and magnetic cores 32 arranged above and below the current collector 7 are It is the cross section (cross section of AA of FIG. 3) cut out along the length direction of a collector.

誘導加熱コイル31及び磁気コア32は、集電体7の上面及び下面から、空気の流れを妨げない程度の間隔を離して配置される。   The induction heating coil 31 and the magnetic core 32 are spaced apart from the upper and lower surfaces of the current collector 7 so as not to interfere with the air flow.

冷却装置4は、ダクト44の吸込み口46付近の外壁に、冷却板41を備える。ダクト44の吸込み口46は、一組の誘導加熱装置3の誘導加熱コイル31の中央に設けられた開口部の上部に配置される。なお、冷却装置4は、ダクト44の吸込み口46付近の内壁に、冷却板41を備えてもよい。   The cooling device 4 includes a cooling plate 41 on the outer wall near the suction port 46 of the duct 44. The suction port 46 of the duct 44 is disposed above the opening provided in the center of the induction heating coil 31 of the set of induction heating devices 3. The cooling device 4 may include a cooling plate 41 on the inner wall near the suction port 46 of the duct 44.

活物質が塗布された集電体7は、上下一組の誘導加熱コイル31の間を通過すると、誘導加熱によって加熱される。このため、集電体7の活物質から溶剤蒸気が発生する。   When the current collector 7 coated with the active material passes between a pair of upper and lower induction heating coils 31, it is heated by induction heating. For this reason, solvent vapor is generated from the active material of the current collector 7.

そして、冷却装置4は、ダクト44の吸い込み口46から、発生した溶剤蒸気を回収する。この場合、集電体7と誘導加熱コイル31との間の隙間から周囲の空気が流れ込むので、冷却装置4は、効率よく溶剤蒸気を吸引することができる。   Then, the cooling device 4 recovers the generated solvent vapor from the suction port 46 of the duct 44. In this case, since the surrounding air flows from the gap between the current collector 7 and the induction heating coil 31, the cooling device 4 can efficiently suck the solvent vapor.

図2で説明したとおり、吸引された溶剤蒸気が冷却板41によって冷却されると、凝結した溶剤は、回収桶43に回収される。   As described with reference to FIG. 2, when the sucked solvent vapor is cooled by the cooling plate 41, the condensed solvent is recovered in the recovery tank 43.

なお、冷却装置4は、外部に備えられた図示しない有機溶剤回収装置に接続されてもよい。この場合、回収桶43が回収した溶剤は、例えば、図示しないパイプ及びポンプを介して有機溶剤回収装置に圧送される。   The cooling device 4 may be connected to an organic solvent recovery device (not shown) provided outside. In this case, the solvent recovered by the recovery tank 43 is pumped to the organic solvent recovery device via, for example, a pipe and a pump (not shown).

また、冷却装置4のダクト44の全部は、誘導加熱乾燥炉2の内部に配置されるのが望ましい。これによって、溶剤蒸気が除去された乾燥空気は、誘導加熱乾燥炉2の内部で還流される。   Further, it is desirable that the entire duct 44 of the cooling device 4 is disposed inside the induction heating drying furnace 2. Thus, the dry air from which the solvent vapor has been removed is refluxed inside the induction heating drying furnace 2.

以上説明したとおり、本実施形態によれば、誘導加熱コイルの直上に配置されたダクトの吸込み口付近を冷却することによって、溶剤蒸気を積極的に凝結させ、凝結した溶剤を回収するので、凝結した溶剤が電極膜に再付着することを防ぐことができる。これによって、均一に乾燥した電極膜を作製することができる。   As described above, according to the present embodiment, by cooling the vicinity of the suction port of the duct disposed immediately above the induction heating coil, the solvent vapor is actively condensed and the condensed solvent is recovered. It is possible to prevent the solvent from reattaching to the electrode film. As a result, a uniformly dried electrode film can be produced.

[実施形態2]
図5は、本発明の第2の実施形態の冷却装置4の配置の例を示す説明図である。
[Embodiment 2]
FIG. 5 is an explanatory diagram showing an example of the arrangement of the cooling device 4 according to the second embodiment of the present invention.

本実施形態の冷却装置4は、図4に示した冷却板41の代わりに、ダクト44の吸込み口46の上部の内壁に冷却フィン42を備える。冷却フィン42は、例えば、多数の冷却用のフィンを備えたコンデンサ等の熱交換器である。なお、冷却装置4は、冷却板、冷却フィン以外の他の装置によって、ダクト44全体を冷却してもよい。   The cooling device 4 of the present embodiment includes cooling fins 42 on the inner wall of the upper portion of the suction port 46 of the duct 44 instead of the cooling plate 41 shown in FIG. The cooling fin 42 is, for example, a heat exchanger such as a condenser having a large number of cooling fins. The cooling device 4 may cool the entire duct 44 by a device other than the cooling plate and the cooling fin.

また、ダクト44は、少なくとも二つのファン45及び少なくとも二つの排気口を備えてもよい。この場合、二つの排気口のうちの一方は、誘導加熱乾燥炉2の内部に配置され、他方は、外部に備えられた図示しない排気濃縮装置に接続されてもよい。   The duct 44 may include at least two fans 45 and at least two exhaust ports. In this case, one of the two exhaust ports may be disposed inside the induction heating drying furnace 2, and the other may be connected to an exhaust concentrator (not shown) provided outside.

そして、有機溶剤を含む一部のガスは、排気濃縮装置に供給され、他の残りのガスは、誘導加熱乾燥炉2の内部に還流される。つまり、全部のガスが誘導加熱乾燥炉2から排気されないので、本実施形態の電極乾燥装置は、外部に備えられる排気濃縮装置の負荷を軽減することができる。   A part of the gas containing the organic solvent is supplied to the exhaust concentrator, and the other remaining gas is returned to the inside of the induction heating drying furnace 2. That is, since all the gas is not exhausted from the induction heating drying furnace 2, the electrode drying apparatus of this embodiment can reduce the load of the exhaust concentration apparatus provided outside.

なお、排気濃縮装置は、誘導加熱乾燥炉2から排気されたガスを、濃縮された有機溶剤を含むガスと有機溶剤を含まないガスとに分離した後、有機溶剤を含まないガスを系外に排出してもよい。また、排気濃縮装置は、図示しない有機溶剤回収装置に接続され、接続された有機溶剤回収装置に濃縮ガスを供給してもよい。   The exhaust concentrator separates the gas exhausted from the induction heating drying furnace 2 into a gas containing a concentrated organic solvent and a gas not containing an organic solvent, and then the gas not containing the organic solvent is taken out of the system. It may be discharged. Further, the exhaust concentration device may be connected to an organic solvent recovery device (not shown) and supply the concentrated gas to the connected organic solvent recovery device.

以上説明したとおり、本実施形態によれば、誘導加熱コイルの直上に配置されたダクトの内部、又はダクト自体を冷却することによって、溶剤蒸気を積極的に凝結させ、凝結した溶剤を回収するので、凝結した溶剤が電極膜に再付着することを防ぐことができる。これによって、均一に乾燥した電極膜を作製することができる。   As described above, according to the present embodiment, by cooling the inside of the duct arranged directly above the induction heating coil or the duct itself, the solvent vapor is actively condensed, and the condensed solvent is recovered. It is possible to prevent the condensed solvent from reattaching to the electrode film. As a result, a uniformly dried electrode film can be produced.

また、冷却装置を通過し、溶剤蒸気が除去された排気の少なくとも一部が、誘導加熱乾燥炉に還流されるので、誘導加熱乾燥炉の外部に配置される排気濃縮装置の負荷を減少させることができる。   In addition, since at least part of the exhaust gas that has passed through the cooling device and from which the solvent vapor has been removed is recirculated to the induction heating drying furnace, the load on the exhaust concentrating device disposed outside the induction heating drying furnace is reduced. Can do.

[実施形態3]
図6は、第3の実施形態の冷却装置4の構成を示す説明図である。
[Embodiment 3]
FIG. 6 is an explanatory diagram illustrating a configuration of the cooling device 4 according to the third embodiment.

第3の実施形態の冷却装置4では、誘導過熱装置3に隣接した位置に、誘導過熱装置3を冷却するための冷却板60が設けられている。冷却板60は、冷却板41と同様の構造、例えば、銅、銅合金等が鍛造又は圧延されたインゴットで構成され、内部に冷却水(冷却媒体)の通路を備え、冷却水(冷却媒体)を供給又は排出するための連結管に接続される構造としてもよいし、冷却板41と異なる構造としてもよい。また、冷却板60を配置する位置も、図6に示す位置に限定されることはない。   In the cooling device 4 of the third embodiment, a cooling plate 60 for cooling the induction superheater 3 is provided at a position adjacent to the induction superheater 3. The cooling plate 60 is configured by an ingot formed by forging or rolling copper, a copper alloy, or the like, similar to the cooling plate 41, and has a cooling water (cooling medium) passage therein, and includes cooling water (cooling medium). It is good also as a structure connected to the connecting pipe for supplying or discharging | emitting, and it is good also as a structure different from the cooling plate 41. FIG. Further, the position where the cooling plate 60 is arranged is not limited to the position shown in FIG.

誘導加熱によって蒸発した溶剤蒸気は、ファン45によって、ダクト44の吸い込み口46から吸引される。この時、冷却板60によって、溶剤蒸気が冷却されて凝結しないように、冷却板60の温度を設定しておく。すなわち、冷却板60の温度は、冷却板41の温度よりも高い。   The solvent vapor evaporated by the induction heating is sucked from the suction port 46 of the duct 44 by the fan 45. At this time, the temperature of the cooling plate 60 is set so that the solvent vapor is cooled and not condensed by the cooling plate 60. That is, the temperature of the cooling plate 60 is higher than the temperature of the cooling plate 41.

以上説明したとおり、第3の実施形態によれば、誘導過熱装置3を冷却する冷却板60を設けたので、誘導加熱装置3を冷却することができる。また、冷却板60の温度を冷却板41の温度よりも高く設定しておくことにより、誘導加熱によって蒸発した溶剤蒸気が冷却板60によって凝結するのを防いで、凝結した溶剤が電極膜に再付着することを防ぐことができる。すなわち、溶剤蒸気は、第1の実施形態と同様に、冷却板41によって冷却されて凝結し、回収桶43によって回収される。   As described above, according to the third embodiment, since the cooling plate 60 for cooling the induction overheating device 3 is provided, the induction heating device 3 can be cooled. Further, by setting the temperature of the cooling plate 60 higher than the temperature of the cooling plate 41, the solvent vapor evaporated by induction heating is prevented from condensing by the cooling plate 60, and the condensed solvent is re-applied to the electrode film. It can be prevented from adhering. That is, the solvent vapor is cooled and condensed by the cooling plate 41 and is recovered by the recovery bar 43 as in the first embodiment.

なお、図6では、図4に示す第1の実施形態の冷却装置4の構成に対して、冷却板60を追加した構成を示したが、図5に示す第2の実施形態の冷却装置4の構成に対して、誘導過熱装置3を冷却するための冷却板60を追加することもできる。   6 shows a configuration in which the cooling plate 60 is added to the configuration of the cooling device 4 of the first embodiment shown in FIG. 4, the cooling device 4 of the second embodiment shown in FIG. A cooling plate 60 for cooling the induction superheater 3 can be added to the configuration.

また、誘導加熱装置3を冷却する手段として、冷却板60を一例に挙げて説明したが、冷却板に限定されることはない。   Moreover, although the cooling plate 60 was mentioned as an example and demonstrated as a means to cool the induction heating apparatus 3, it is not limited to a cooling plate.

1 塗工機
2 誘導加熱乾燥炉(電極乾燥室)
3 誘導加熱装置(誘導加熱手段)
4 冷却装置
7 集電体(電極箔)
8 移送装置
31 誘導加熱コイル
41 冷却板(冷却手段、第一の冷却手段)
42 冷却フィン(冷却手段、第一の冷却手段)
43 回収桶(回収手段)
44 ダクト
45 ファン
46 吸込み口
60 冷却板(第二の冷却手段)
1 Coating machine 2 Induction heating drying furnace (electrode drying room)
3 Induction heating device (induction heating means)
4 Cooling device 7 Current collector (electrode foil)
8 Transfer device 31 Induction heating coil 41 Cooling plate (cooling means, first cooling means)
42 Cooling fins (cooling means, first cooling means)
43 Collection dredging (collection means)
44 Duct 45 Fan 46 Suction port 60 Cooling plate (second cooling means)

Claims (8)

活物質が塗布された電極箔を乾燥させる電極乾燥装置であって、
誘導加熱によって前記電極箔を加熱する誘導加熱手段と、
前記誘導加熱手段によって前記電極箔から蒸発した溶剤蒸気を凝結させる冷却手段と、
前記冷却手段によって凝結した溶剤を回収する回収手段と、
前記誘導加熱手段、前記冷却手段及び前記回収手段を格納する電極乾燥室と、
を備えることを特徴とする電極乾燥装置。
An electrode drying apparatus for drying an electrode foil coated with an active material,
Induction heating means for heating the electrode foil by induction heating;
A cooling means for condensing solvent vapor evaporated from the electrode foil by the induction heating means;
Recovery means for recovering the solvent condensed by the cooling means;
An electrode drying chamber for storing the induction heating means, the cooling means, and the recovery means;
An electrode drying apparatus comprising:
前記冷却手段は、前記誘導加熱手段の近傍に配置され、
前記回収手段は、前記冷却手段の鉛直下方に配置されることを特徴とする請求項1に記載の電極乾燥装置。
The cooling means is disposed in the vicinity of the induction heating means,
The electrode drying apparatus according to claim 1, wherein the recovery unit is disposed vertically below the cooling unit.
前記電極乾燥装置は、さらに、前記蒸発した溶剤蒸気を吸引するダクトを備え、
前記冷却手段は、前記ダクトの内部に配置され、
前記回収手段は、前記ダクトの鉛直下方に配置されることを特徴とする請求項1又は2に記載の電極乾燥装置。
The electrode drying apparatus further includes a duct for sucking the evaporated solvent vapor,
The cooling means is disposed inside the duct;
The electrode drying apparatus according to claim 1, wherein the recovery unit is disposed vertically below the duct.
前記電極乾燥装置は、さらに、前記蒸発した溶剤蒸気を吸引するダクトを備え、
前記冷却手段は、前記ダクトの外壁を冷却するように配置され、
前記回収手段は、前記ダクトの鉛直下方に配置されることを特徴とする請求項1又は2に記載の電極乾燥装置。
The electrode drying apparatus further includes a duct for sucking the evaporated solvent vapor,
The cooling means is arranged to cool the outer wall of the duct;
The electrode drying apparatus according to claim 1, wherein the recovery unit is disposed vertically below the duct.
前記冷却装置を通過した空気の一部又は全部を、前記電極乾燥室内に戻すことを特徴とする請求項1から4のいずれか一つに記載の電極乾燥装置。   5. The electrode drying apparatus according to claim 1, wherein part or all of the air that has passed through the cooling device is returned to the electrode drying chamber. 前記誘導加熱手段は、概略矩形状の誘導加熱コイルを備え、
前記ダクトは、前記概略矩形状の誘導加熱コイルの中央上面に配置されることを特徴とする請求項3又は4に記載の電極乾燥装置。
The induction heating means includes a substantially rectangular induction heating coil,
The electrode drying apparatus according to claim 3, wherein the duct is disposed on a central upper surface of the substantially rectangular induction heating coil.
活物質が塗布された電極箔を乾燥させる電極乾燥装置であって、
誘導加熱によって前記電極箔を加熱する誘導加熱手段と、
前記誘導加熱手段によって前記電極箔から蒸発した溶剤蒸気を凝結させる第一の冷却手段と、
前記第一の冷却手段によって凝結した溶剤を回収する回収手段と、
前記誘導過熱手段を冷却する第二の冷却手段と、
前記誘導加熱手段、前記第一の冷却手段、前記第二の冷却手段及び前記回収手段を格納する電極乾燥室と、
を備え、
前記第一の冷却手段は、前記第二の冷却手段よりも温度が低いことを特徴とする電極乾燥装置。
An electrode drying apparatus for drying an electrode foil coated with an active material,
Induction heating means for heating the electrode foil by induction heating;
First cooling means for condensing solvent vapor evaporated from the electrode foil by the induction heating means;
A recovery means for recovering the solvent condensed by the first cooling means;
A second cooling means for cooling the induction superheating means;
An electrode drying chamber for storing the induction heating means, the first cooling means, the second cooling means, and the recovery means;
With
The electrode drying apparatus characterized in that the first cooling means has a temperature lower than that of the second cooling means.
電極乾燥室内において、活物質が塗布された電極箔を乾燥させる電極乾燥方法であって、
誘導加熱によって前記電極箔を加熱し、
前記加熱された電極箔から蒸発した溶剤蒸気を冷却することによって凝結させ、
前記凝結した溶剤を回収することを特徴とする電極乾燥方法。
An electrode drying method for drying an electrode foil coated with an active material in an electrode drying chamber,
Heating the electrode foil by induction heating,
Condensing by cooling the solvent vapor evaporated from the heated electrode foil;
An electrode drying method, wherein the condensed solvent is recovered.
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