JP2015077698A - Kneading machine - Google Patents

Kneading machine Download PDF

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JP2015077698A
JP2015077698A JP2013214858A JP2013214858A JP2015077698A JP 2015077698 A JP2015077698 A JP 2015077698A JP 2013214858 A JP2013214858 A JP 2013214858A JP 2013214858 A JP2013214858 A JP 2013214858A JP 2015077698 A JP2015077698 A JP 2015077698A
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kneading
electrode mixture
filter
container
tank
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JP6115436B2 (en
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建志 岡村
Kenji Okamura
建志 岡村
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Toyota Industries Corp
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Abstract

PROBLEM TO BE SOLVED: To remove lump from obtained kneaded object without adding a piping and a pump between a kneading machine and a coater.SOLUTION: A kneading machine 10 comprises: a tank formed of a tank body 11a storing raw materials including at least an active material, a binder and a solvent and a hood 11b; kneading means 12 for kneading the raw materials in the tank body 11a; and a discharge part 13 for discharging the raw materials after being kneaded in the tank body 11a. The discharge part 13 has a filter 14 for filtering a slurry-state mixture for electrode which passes the discharge part 13.

Description

本発明は、混練機に係り、詳しくは蓄電装置の電極用合剤を製造するための混練機に関する。   The present invention relates to a kneading machine, and more particularly to a kneading machine for producing an electrode mixture for a power storage device.

二次電池やキャパシタのような蓄電装置は再充電が可能であり、繰り返し使用することができるため電源として広く利用されている。従来から、EV(Electric Vehicle)やPHV(Plug-in Hybrid Vehicle)などの車両に搭載される蓄電装置としては、リチウムイオン二次電池や、ニッケル水素二次電池などがよく知られている。これらの二次電池では、金属箔の表面に活物質を含むペースト状又はスラリー状の活物質合剤を塗布して活物質層を形成した電極を、間にセパレータを介在させた状態で積層又は捲回するなどして電極組立体を形成するとともに、該電極組立体をケースに収容している。   Power storage devices such as secondary batteries and capacitors are widely used as power sources because they can be recharged and can be used repeatedly. Conventionally, lithium ion secondary batteries, nickel-hydrogen secondary batteries, and the like are well known as power storage devices mounted on vehicles such as EVs (Electric Vehicles) and PHVs (Plug-in Hybrid Vehicles). In these secondary batteries, an electrode having an active material layer formed by applying a paste-like or slurry-like active material mixture containing an active material on the surface of a metal foil is laminated with a separator interposed therebetween. The electrode assembly is formed by winding or the like, and the electrode assembly is housed in a case.

スラリー状の電極用活物質合剤(以下、単に電極用合剤と称す)の調整は、少なくとも活物質、バインダ及び溶媒を含み、必要に応じて増粘剤を含む原材料を混練する。活物質、バインダ及び増粘剤は粉体であり、粉体と溶媒とを均一に混合してスラリー状の活物質合剤を製造するため、例えば、少量の溶媒で活物質等の粉体を混練(固練り)し、次いで溶媒で希釈する混練方法が用いられている。   Adjustment of a slurry-like electrode active material mixture (hereinafter simply referred to as electrode mixture) includes at least an active material, a binder and a solvent, and kneads a raw material containing a thickener as necessary. The active material, the binder, and the thickener are powders, and the powder and solvent are uniformly mixed to produce a slurry-like active material mixture. A kneading method (kneading) followed by dilution with a solvent is used.

混練方法としてバッチ式と連続式とがある。連続式では、内部に攪拌体が設けられたケーシング内に導入口から連続的に原料が供給され、攪拌体により攪拌混合された後、排出口から排出される。例えば、特許文献1には、二軸連続混練機として、混練室内に二本の回転軸を配置し、回転軸に支持された送りスクリューにより投入される粉体及び液体を上流より下流に送りながら、同様に回転軸に支持されたバレル(攪拌体)にて粉体及び液体を攪拌する構造が記載されている。また、このような混練機を含む電極製造装置の例が、特許文献2に開示されている。特許文献2の電極製造装置は、製造部・貯蔵部・塗工部よりなり、各部は管路とポンプとで接続されている。一方、バッチ式では、混練機のタンク内で1回分の原材料の混練が終わると、タンクの回収口(排出口)からスラリー状の電極用合剤を回収して塗工機(塗布装置)で使用する。このようなバッチ式の混練機の一例として、特許文献3には、容器内のペーストに対し、蓋とともに混練手段を昇降可能した構成が開示されている。   There are batch and continuous kneading methods. In the continuous type, the raw material is continuously supplied from the introduction port into the casing provided with the stirring body therein, and after being stirred and mixed by the stirring body, is discharged from the discharge port. For example, in Patent Document 1, as a biaxial continuous kneader, two rotating shafts are arranged in a kneading chamber, and powder and liquid charged by a feed screw supported by the rotating shaft are fed from upstream to downstream. Similarly, a structure is described in which powder and liquid are stirred by a barrel (stirring body) supported by a rotating shaft. An example of an electrode manufacturing apparatus including such a kneader is disclosed in Patent Document 2. The electrode manufacturing apparatus of patent document 2 consists of a manufacturing part, a storage part, and a coating part, and each part is connected with the pipe line and the pump. On the other hand, in the batch type, once the kneading of the raw materials is completed in the tank of the kneader, the slurry-like electrode mixture is recovered from the recovery port (discharge port) of the tank. use. As an example of such a batch-type kneader, Patent Document 3 discloses a configuration in which the kneading means can be lifted and lowered together with the lid with respect to the paste in the container.

バッチ式と連続式とを比較した場合、バッチ式はトレーサビリティーに優れる。電極用合剤にて例えると、連続式の混練機は、連続して投入される粉体及び液体の各材料と、排出口から排出される電極用合剤との関係が、構造上、確認しづらい。具体的には、製造された電極用合剤、あるいは電極の活物質層の特性に変化があった場合にも、何時投入された、どの材料が関係するのか、特定することが困難である。このため、混練時の品質管理を重視する場合には、バッチ式が用いられている。   When the batch type and the continuous type are compared, the batch type is excellent in traceability. For example, in a continuous kneading machine, the relationship between the powder and liquid materials that are continuously charged and the electrode mixture discharged from the discharge port is confirmed structurally. difficult. Specifically, even when there is a change in the characteristics of the manufactured electrode mixture or the active material layer of the electrode, it is difficult to specify when and which material is charged. For this reason, when importance is attached to quality control at the time of kneading, a batch type is used.

特開2011−83703号公報JP 2011-83703 A 特開2011−181465号公報JP 2011-181465 A 特開2009−22890号号公報JP 2009-22890 A

バッチ式の混練機において、より品質の高い電極用合剤を得る為には、混練後にダマ(粉体の凝集塊)を取り除くことが望ましい。特許文献2には、貯蔵部内にて、電極スラリーを循環させる循環系と、循環系の配置された粗粒除去フィルタとが開示されている。しかしながら、バッチ式の混練機は、特許文献2のようなフィルタを配置する為の配管、および、電極用合剤をフィルタに送るポンプを有していない。   In a batch kneader, it is desirable to remove lumps (aggregates of powder) after kneading in order to obtain a higher quality electrode mixture. Patent Document 2 discloses a circulation system that circulates an electrode slurry in a storage unit and a coarse particle removal filter in which the circulation system is arranged. However, the batch-type kneader does not have a pipe for arranging the filter as in Patent Document 2 and a pump for feeding the electrode mixture to the filter.

本発明は、前記の問題に鑑みてなされたものであって、その目的は、混練機と塗工機との間に配管やポンプを設けたりすることなく、ダマを除去することができるバッチ式の混練機を提供することにある。   The present invention has been made in view of the above problems, and its purpose is a batch type capable of removing lumps without providing a pipe or a pump between the kneading machine and the coating machine. Is to provide a kneading machine.

上記課題を解決する混練機は、複数の原材料より混練物を製造する混練機であって、前記原材料を収容する容器と、前記容器内で前記原材料を混練する混練手段と、前記容器内より混練物を排出することができる排出部と、前記排出部に設けられたフィルタとを備えている。   A kneading machine that solves the above problems is a kneading machine that produces a kneaded material from a plurality of raw materials, a container that contains the raw materials, a kneading means that kneads the raw materials in the container, and kneading from within the container. A discharge unit capable of discharging an object, and a filter provided in the discharge unit.

この混練機によれば、容器内に原材料を投入すると、混練手段により混練され混練物が製造される。混練物は、排出部から排出(回収)される際、排出部に設けられたフィルタを通過することによりダマが除去される。したがって、混練機と塗工機との間の配管やポンプを設けたりすることなく、ろ過の為に作業を新たに追加すること無く、得られた混練物からダマを除去することができる。   According to this kneading machine, when the raw materials are put into the container, the kneaded product is kneaded by the kneading means. When the kneaded material is discharged (collected) from the discharge portion, the kneaded material is removed by passing through a filter provided in the discharge portion. Therefore, it is possible to remove lumps from the obtained kneaded product without providing piping or a pump between the kneading machine and the coating machine, and without adding a new operation for filtration.

前記混練物は少なくとも活物質、バインダおよび溶媒を原材料として含む電極用合剤であり、前記排出部は前記フィルタより容器内側に配置された開閉手段を備え、前記開閉手段は、閉鎖時に、前記原材料の前記フィルタへの侵入を阻止することが好ましい。容器内の原材料を混練手段で混練する際、原材料がフィルタと接触する状態で混練されると、混練中に原材料の粉末がフィルタに侵入する。フィルタに侵入した原材料は、混練手段によるせん断作用を受けない為、生成される電極用合剤の分散状態が悪化する虞がある。しかし、排出部にて、フィルタより容器内側に開閉手段を配置することで、混練中にフィルタへの原材料の侵入が阻止される。これにより、スラリー状の電極用合剤における活物質の分散状態が悪化する虞がなくなる。   The kneaded material is an electrode mixture containing at least an active material, a binder, and a solvent as raw materials, and the discharge portion includes opening / closing means disposed on the inner side of the container than the filter, and the opening / closing means includes the raw material when closed. It is preferable to prevent intrusion into the filter. When the raw materials in the container are kneaded by the kneading means, if the raw materials are kneaded in contact with the filter, the raw material powder enters the filter during the kneading. Since the raw material that has entered the filter is not subjected to a shearing action by the kneading means, there is a possibility that the dispersed state of the generated electrode mixture may deteriorate. However, by disposing the opening / closing means inside the container from the filter at the discharge portion, entry of raw materials into the filter is prevented during kneading. Thereby, there is no possibility that the dispersion state of the active material in the slurry-like electrode mixture is deteriorated.

前記容器は、前記容器の上部に、前記容器内へのガスの導入を可能とする供給口を備えることが好ましい。この構成によれば、原材料の混練終了後、スラリー状の電極用合剤を排出部から排出(回収)する際、供給口から加圧ガスを容器内に供給することにより、排出部にフィルタを配置したとしても、電極用合剤の排出(回収)に要する時間を短くすることができる。   It is preferable that the container includes a supply port that allows gas to be introduced into the container at an upper part of the container. According to this configuration, when the slurry-like electrode mixture is discharged (recovered) from the discharge portion after the raw materials have been kneaded, the pressurized gas is supplied into the container from the supply port, whereby the filter is provided at the discharge portion. Even if it is arranged, the time required for discharging (collecting) the electrode mixture can be shortened.

本発明によれば、混練機と塗工機との間に、配管やポンプを追加すること無く、得られた混練物からダマを除去することができる。   According to the present invention, it is possible to remove lumps from the obtained kneaded product without adding piping or a pump between the kneading machine and the coating machine.

(a)は一実施形態の混練機の一部破断正面図、(b)は部分拡大断面図。(A) is a partially broken front view of the kneading machine of one Embodiment, (b) is a partial expanded sectional view. 混練手段が混練位置に配置された状態の模式断面図。The schematic cross section of the state where the kneading means is disposed at the kneading position. (a)は電極用合剤の回収時に配管を接続した状態の模式部分断面図、(b)はカバーを開位置に配置して電極用合剤を回収している状態の模式部分断面図。(A) is a typical fragmentary sectional view of the state which connected piping at the time of collection | recovery of the electrode mixture, (b) is a schematic fragmentary sectional view of the state which has arrange | positioned the cover in the open position and collect | recovered the electrode mixture. (a)は別の実施形態の模式部分断面図、(b)はその部分拡大図。(A) is a typical fragmentary sectional view of another embodiment, (b) is the elements on larger scale. 別の実施形態の模式部分断面図。The typical fragmentary sectional view of another embodiment. 別の実施形態の模式部分断面図。The typical fragmentary sectional view of another embodiment. 別の実施形態の模式部分断面図。The typical fragmentary sectional view of another embodiment.

以下、本発明を具体化した一実施形態を図1〜図3にしたがって説明する。
図1に示すように、バッチ式の混練機10は、基本的にプラネタリーミキサーと同様に構成され、原材料を収容する容器として、有底円筒状のタンク本体11aと、タンク11の上部にてタンク本体11aの開口部を覆う有天円筒状のフード11bとで構成されたタンク11と、タンク本体11aに収容された原材料を混練する混練手段12とを備えている。タンク本体11aは、タンク本体11a内で混練された後の原材料を排出する排出部13を備え、排出部13には、排出部13を通過する電極用合剤をろ過するフィルタ14が設けられている。タンク11は、ステンレス等の金属製である。
Hereinafter, an embodiment embodying the present invention will be described with reference to FIGS.
As shown in FIG. 1, the batch-type kneader 10 is basically configured in the same manner as a planetary mixer, and has a bottomed cylindrical tank body 11 a and a top of the tank 11 as containers for containing raw materials. A tank 11 composed of a hooded cylindrical hood 11b covering the opening of the tank body 11a and a kneading means 12 for kneading the raw materials stored in the tank body 11a are provided. The tank body 11a includes a discharge portion 13 that discharges the raw material after being kneaded in the tank body 11a, and the discharge portion 13 is provided with a filter 14 that filters the electrode mixture that passes through the discharge portion 13. Yes. The tank 11 is made of metal such as stainless steel.

タンク11の上方には、攪拌ヘッド15がシリンダ16により昇降可能に設けられており、フード11bは、攪拌ヘッド15と共に昇降可能に攪拌ヘッド15に固定されている。フード11bは、タンク11内へのガスの導入を可能とする供給口としての加圧口17を備えている。加圧口17は、パイプを介して加圧ガス供給部に接続可能に構成されている。即ち、タンク11は、タンク11内を加圧する加圧ガス供給部に接続可能な加圧口17を備えている。   Above the tank 11, a stirring head 15 is provided so as to be movable up and down by a cylinder 16, and the hood 11 b is fixed to the stirring head 15 so as to be movable up and down together with the stirring head 15. The hood 11 b includes a pressurizing port 17 as a supply port that enables introduction of gas into the tank 11. The pressurizing port 17 is configured to be connectable to a pressurized gas supply unit via a pipe. That is, the tank 11 includes a pressurizing port 17 that can be connected to a pressurized gas supply unit that pressurizes the inside of the tank 11.

攪拌ヘッド15はロータ18を備え、ロータ18はモータ19により減速機20を介して駆動される駆動軸により駆動される。ロータ18は遊星歯車機構を備え、混練手段12はロータ18により遊星歯車運動を行う状態で駆動される。   The stirring head 15 includes a rotor 18, and the rotor 18 is driven by a drive shaft that is driven by a motor 19 via a speed reducer 20. The rotor 18 includes a planetary gear mechanism, and the kneading means 12 is driven by the rotor 18 in a state of performing planetary gear movement.

混練手段12は、攪拌ヘッド15の昇降により、タンク本体11a内で攪拌を行う攪拌位置(図2の状態)及びタンク本体11a内から退出した待機位置に移動可能になっている。混練手段12は複数(この実施形態では2個)のブレード12aを有し、攪拌ヘッド15が最下降位置に移動した状態で、ブレード12aがタンク本体11a内の被攪拌物の量の多少に限らず、被攪拌物を攪拌可能な攪拌位置に配置される。混練手段12は攪拌位置において、タンク本体11a内で遊星運動を行いながら、粉体の混合あるいは粉体と液体との混練が可能に構成されている。   The kneading means 12 can be moved to a stirring position (the state shown in FIG. 2) for stirring in the tank body 11a and a standby position retracted from the tank body 11a by raising and lowering the stirring head 15. The kneading means 12 has a plurality (two in this embodiment) of blades 12a, and the blade 12a is limited to the amount of the object to be stirred in the tank main body 11a with the stirring head 15 moved to the lowest position. First, the stirring object is disposed at a stirring position where stirring is possible. The kneading means 12 is configured to be able to mix powder or knead powder and liquid while performing a planetary motion in the tank body 11a at the stirring position.

ブレード12aは、例えば、ステンレス等の金属製の角材を繋ぎ合わせて三角枠状に形成されている。また、ブレード12aは、混練手段12が攪拌位置に配置された状態において、タンク本体11aの底壁内面との間において原材料に大きなせん断力を作用させる距離を有するように配設されている。   The blade 12a is formed in a triangular frame shape by joining, for example, metal squares such as stainless steel. Further, the blade 12a is disposed so as to have a distance for applying a large shearing force to the raw material between the blade 12a and the inner surface of the bottom wall of the tank body 11a in a state where the kneading means 12 is disposed at the stirring position.

図1(b)に示すように、排出部13は、タンク本体11aの底壁21に形成された開口部13aと、開口部13aの周縁からタンク本体11aの外側に突設された筒部13bとを備えている。筒部13bの基端側には開口部13aを通過する混練された後の原材料、即ち電極用合剤(電極用活物質合剤)をろ過するフィルタ14が設けられている。   As shown in FIG.1 (b), the discharge part 13 has the opening part 13a formed in the bottom wall 21 of the tank main body 11a, and the cylinder part 13b protrudingly provided by the outer periphery of the tank main body 11a from the periphery of the opening part 13a. And. A filter 14 is provided on the proximal end side of the cylindrical portion 13b to filter the kneaded raw material that passes through the opening 13a, that is, the electrode mixture (electrode active material mixture).

排出部13は、排出部13の開閉手段であり、フィルタ14を覆うカバー23を備えている。カバー23は、開口部13aにおけるフィルタ14が設けられた位置よりタンク本体11aの内側寄りに設けられている。カバー23は、タンク本体11a内に存在する原材料が排出部13に侵入するのを阻止する図1(b)に示す遮蔽位置と、原材料が排出部13に進入するのを許容する退避位置とに移動可能に設けられている。   The discharge unit 13 is an opening / closing unit for the discharge unit 13 and includes a cover 23 that covers the filter 14. The cover 23 is provided closer to the inside of the tank body 11a than the position where the filter 14 is provided in the opening 13a. The cover 23 has a shielding position shown in FIG. 1B that prevents the raw material existing in the tank main body 11 a from entering the discharge portion 13 and a retreat position that allows the raw material to enter the discharge portion 13. It is provided to be movable.

詳述すると、底壁21にはカバー23をタンク本体11aの底面と平行にスライド可能に収容する収容部24が設けられている。カバー23は、開口部13aの径より幅広に形成され、底壁21には収容部24の開口部13a寄り端部に連続してカバー23の移動を許容するガイド溝25が形成されている。そして、図1(b)に示すように、カバー23は、遮蔽位置に配置された状態では、先端がガイド溝25の収容部24と対向する箇所に嵌合するようになっている。   More specifically, the bottom wall 21 is provided with an accommodating portion 24 that accommodates the cover 23 so as to be slidable parallel to the bottom surface of the tank body 11a. The cover 23 is formed wider than the diameter of the opening 13a, and a guide groove 25 that allows the movement of the cover 23 is formed in the bottom wall 21 continuously to the end of the accommodating portion 24 near the opening 13a. As shown in FIG. 1 (b), the cover 23 is adapted to be fitted at a position where the tip of the cover 23 faces the accommodating portion 24 of the guide groove 25 in the state where the cover 23 is disposed at the shielding position.

収容部24には底壁21の外面側に開口する溝24aが形成されている。カバー23にはその後端側、図1(b)における右端側に、棒状の操作部材26が溝24aを貫通する状態で固定されている。そして、カバー23は、作業者が操作部材26を溝24aに沿って移動させることにより、図1(b)に示す遮蔽位置と、カバー23が開口部13aを開放する図3(b)に示す退避位置とに移動されるようになっている。なお、収容部24の開口部13a寄りの端部には、タンク本体11a内に収容された原材料が溝24aから外部に漏洩するのを防止するシール部材27が設けられている。   A groove 24 a that opens to the outer surface side of the bottom wall 21 is formed in the accommodating portion 24. A rod-like operation member 26 is fixed to the cover 23 on the rear end side, on the right end side in FIG. The cover 23 is shown in FIG. 3B where the operator moves the operating member 26 along the groove 24a, and in FIG. 3B where the cover 23 opens the opening 13a. It is moved to the retracted position. A seal member 27 for preventing the raw material stored in the tank body 11a from leaking to the outside from the groove 24a is provided at the end of the storage portion 24 near the opening 13a.

次に前記のように構成された混練機10の作用を、二次電池であるリチウムイオン電池の正極用合剤の製造を例として説明する。
正極用合剤の原材料は、例えば、リチウム・マンガン複合酸化物、リチウム・コバルト複合酸化物、リチウム・ニッケル複合酸化物等の、リチウムと遷移金属との金属複合酸化物からなる正極活物質と、アセチレンブラック等の導電剤と、ポリフッ化ビニリデン(PVDF)等のバインダと、N−メチルピロリドン(NMP)等の溶媒とを含む。
Next, the operation of the kneader 10 configured as described above will be described by taking as an example the production of a positive electrode mixture for a lithium ion battery, which is a secondary battery.
The raw material of the positive electrode mixture is, for example, a positive electrode active material made of a metal composite oxide of lithium and a transition metal, such as a lithium / manganese composite oxide, a lithium / cobalt composite oxide, or a lithium / nickel composite oxide, A conductive agent such as acetylene black, a binder such as polyvinylidene fluoride (PVDF), and a solvent such as N-methylpyrrolidone (NMP) are included.

原材料を混練する場合は、図1(a)に示すように、フード11bが上昇位置に配置されてタンク本体11aが開放され、かつ図1(b)に示すように、カバー23が遮蔽位置に配置された状態で、タンク本体11a内に原材料を収容(投入)する。このとき原材料のうち液体(溶媒)がタンク本体11aに入れられた状態で粉体を投入するのが好ましい。なお、混練は固練りを行った後、さらに溶媒を加えて混練を行うため、溶媒の量は調整完了時に電極用合剤31に含まれる溶媒の量より少ない量が投入される。   When kneading raw materials, as shown in FIG. 1 (a), the hood 11b is placed in the raised position, the tank body 11a is opened, and as shown in FIG. 1 (b), the cover 23 is in the shielding position. The raw material is accommodated (injected) in the tank main body 11a in the arranged state. At this time, it is preferable to add the powder in a state where the liquid (solvent) of the raw materials is placed in the tank body 11a. In addition, since kneading is performed after solid kneading and further kneading by adding a solvent, the amount of the solvent is smaller than the amount of the solvent contained in the electrode mixture 31 when the adjustment is completed.

次にシリンダ16が駆動され、図2に示すように、タンク11は、タンク本体11aをフード11bが覆うとともに、混練手段12のブレード12aが原材料30を混練可能な状態に配置される。その状態でモータ19が駆動されて、ブレード12aが遊星運動を行いつつ自転することにより、原材料30が混練されて固練りが行われる。予め設定された所定時間混練が行われてモータ19が停止される。そして、フード11bが開放位置に配置されて溶媒が追加されて、フード11bが再び開口部を覆う位置に配置された後、混練が再開される。そして、所定時間混練が継続されて電極用合剤31の調整が完了する。   Next, the cylinder 16 is driven, and as shown in FIG. 2, the tank 11 is disposed in a state in which the hood 11 b covers the tank body 11 a and the blade 12 a of the kneading means 12 can knead the raw material 30. In this state, the motor 19 is driven and the blade 12a rotates while performing planetary motion, whereby the raw material 30 is kneaded and kneaded. Kneading is performed for a predetermined time set in advance, and the motor 19 is stopped. Then, after the hood 11b is arranged at the open position, the solvent is added, and the hood 11b is arranged again at a position covering the opening, kneading is resumed. Then, the kneading is continued for a predetermined time, and the adjustment of the electrode mixture 31 is completed.

タンク11内の原材料30を混練手段12で混練する際、原材料30がフィルタ14と接触する状態で混練されると、混練中に粉末や粉末と溶媒との混合物がフィルタ14に侵入する。フィルタ14に侵入した粉末や混合物は、ブレード12aのせん断作用を受けない為、製造される正極用合剤、あるいは電極の活物質層の分散状態が悪化する虞がある。しかし、混練は、フィルタ14と、混練中の原材料30との接触を阻止する遮蔽位置にカバー23が配置されている状態で行われるため、混練中に粉末や粉末と溶媒との混合物がフィルタ14に侵入することが回避され、正極用合剤の分散状態が悪化する虞がない。   When the raw material 30 in the tank 11 is kneaded by the kneading means 12, if the raw material 30 is kneaded in contact with the filter 14, the powder or a mixture of the powder and the solvent enters the filter 14 during the kneading. Since the powder or mixture that has entered the filter 14 is not subjected to the shearing action of the blade 12a, the dispersion of the produced positive electrode mixture or the active material layer of the electrode may be deteriorated. However, since the kneading is performed in a state where the cover 23 is disposed at a shielding position that prevents contact between the filter 14 and the raw material 30 being kneaded, a powder or a mixture of the powder and the solvent is mixed with the filter 14 during the kneading. Intrusion into the cathode is avoided, and there is no possibility that the dispersion state of the positive electrode mixture deteriorates.

原材料30の混練が終了してスラリー状の電極用合剤31の調整が完了すると、タンク本体11a内のスラリー状の電極用合剤31が排出部13から排出(回収)される。先ず、図3(a)に示すように、筒部13bにパイプ28の第1端部が接続される。パイプ28の第2端部は、塗工機の活物質合剤貯留タンクに電極用合剤31を供給する位置に配置される。次に作業者がカバー23の操作部材26を持ってカバー23を退避位置に移動させると、図3(b)に示すように、電極用合剤31がタンク本体11a内から排出部13を介してパイプ28内へ移動する。   When the kneading of the raw material 30 is completed and the adjustment of the slurry-like electrode mixture 31 is completed, the slurry-like electrode mixture 31 in the tank main body 11a is discharged (collected) from the discharge portion 13. First, as shown to Fig.3 (a), the 1st end part of the pipe 28 is connected to the cylinder part 13b. The second end of the pipe 28 is disposed at a position where the electrode mixture 31 is supplied to the active material mixture storage tank of the coating machine. Next, when the operator holds the operating member 26 of the cover 23 and moves the cover 23 to the retracted position, as shown in FIG. 3 (b), the electrode mixture 31 passes from the tank body 11 a through the discharge portion 13. Move into the pipe 28.

タンク本体11a内から排出部13を介してパイプ28内へ移動する電極用合剤31は、排出部13に設けられたフィルタ14を通過し、フィルタ14により電極用合剤31中に存在するダマがろ過されて、ダマが除去される。   The electrode mixture 31 that moves from the tank body 11 a into the pipe 28 through the discharge portion 13 passes through the filter 14 provided in the discharge portion 13, and the filter 14 causes a dama present in the electrode mixture 31. Is filtered to remove lumps.

カバー23を退避位置に移動させた後、加圧口17から加圧ガスをタンク11内に供給する。加圧ガスとしては、例えば、窒素ガスや乾燥空気が使用される。排出部13がタンク本体11aの底壁21に設けられているため、カバー23が退避位置に移動されると、電極用合剤31は自重でタンク本体11a内からパイプ28へと移動する。しかし、加圧口17から加圧ガスをタンク11内に供給することにより、電極用合剤31の排出(回収)に要する時間を短くすることができる。   After the cover 23 is moved to the retracted position, pressurized gas is supplied into the tank 11 from the pressure port 17. For example, nitrogen gas or dry air is used as the pressurized gas. Since the discharge part 13 is provided in the bottom wall 21 of the tank main body 11a, when the cover 23 is moved to the retracted position, the electrode mixture 31 moves from the tank main body 11a to the pipe 28 by its own weight. However, the time required to discharge (collect) the electrode mixture 31 can be shortened by supplying the pressurized gas from the pressure port 17 into the tank 11.

電極用合剤31の回収が終了した後、加圧ガスの供給が停止される。その後、フード11bが上昇位置に移動され、少なくともフィルタ14が洗浄される。その結果、電極用合剤31の回収時に、フィルタ14を通過する電極用合剤31から分離されてフィルタ14上に付着したダマ等が除去されて、次回における電極用合剤31の回収時にフィルタ14が正常に機能する。   After the collection of the electrode mixture 31 is completed, the supply of the pressurized gas is stopped. Thereafter, the hood 11b is moved to the raised position, and at least the filter 14 is washed. As a result, when collecting the electrode mixture 31, the lumps and the like separated from the electrode mixture 31 passing through the filter 14 and adhering to the filter 14 are removed. 14 functions normally.

この実施形態によれば、以下に示す効果を得ることができる。
(1)混練機10は複数の原材料より混練物を製造するバッチ式の混練機であって、原材料30を収容するタンク11と、タンク11内で原材料30を混練する混練手段12と、タンク11内で混練された後の原材料30を排出する排出部13と、排出部13に設けられて、排出部13を通過する混練された後の原材料30である電極用合剤31をろ過するフィルタ14とを備えている。この構成によれば、混練機10と塗工機との間の配管およびポンプを設けたりすることなく、ろ過の為の作業を新たに追加すること無く、得られたスラリー状の電極用合剤31からダマを除去することができる。
According to this embodiment, the following effects can be obtained.
(1) The kneading machine 10 is a batch type kneading machine for producing a kneaded product from a plurality of raw materials. The tank 11 accommodates the raw material 30; the kneading means 12 for kneading the raw material 30 in the tank 11; The discharge part 13 which discharges the raw material 30 after being kneaded inside, and the filter 14 which is provided in the discharge part 13 and filters the electrode mixture 31 which is the raw material 30 after kneading that passes through the discharge part 13. And. According to this configuration, the slurry-like electrode mixture obtained without adding piping and a pump between the kneading machine 10 and the coating machine and without newly adding a work for filtration. The lumps can be removed from 31.

(2)混練機10は、フィルタ14と、混練中の原材料30との接触を阻止するカバー23を備え、カバー23は、タンク11内に存在する原材料30が排出部13に侵入するのを阻止する遮蔽位置と、原材料30が排出部13に進入するのを許容する退避位置とに移動可能に設けられている。この構成によれば、原材料30の混練中にカバー23が遮蔽位置に配置されることにより、混練中に粉末がフィルタ14に侵入することが回避され、スラリー状の電極用合剤31の分散状態が悪化する虞がなくなる。   (2) The kneading machine 10 includes a cover 23 that prevents the filter 14 from contacting the raw material 30 being kneaded. The cover 23 prevents the raw material 30 existing in the tank 11 from entering the discharge unit 13. It is provided so as to be movable between a shielding position where the raw material 30 is moved and a retreat position where the raw material 30 is allowed to enter the discharge portion 13. According to this configuration, the cover 23 is disposed at the shielding position during the kneading of the raw material 30, thereby preventing the powder from entering the filter 14 during the kneading and the dispersed state of the slurry-like electrode mixture 31. There is no risk of deterioration.

(3)タンク11は、タンク11内を加圧する加圧ガス供給部に接続可能な加圧口17を備えている。この構成によれば、原材料30の混練終了後、スラリー状の電極用合剤31を排出部13から排出(回収)する際、加圧口17から加圧ガスをタンク11内に供給することができる。これにより、排出部13にフィルタ14を取付けた場合にも、電極用合剤31の排出(回収)に要する時間を短くすることができる。   (3) The tank 11 includes a pressurizing port 17 that can be connected to a pressurized gas supply unit that pressurizes the inside of the tank 11. According to this configuration, when the slurry-like electrode mixture 31 is discharged (collected) from the discharge unit 13 after the kneading of the raw material 30, the pressurized gas can be supplied into the tank 11 from the pressure port 17. it can. Thereby, also when the filter 14 is attached to the discharge part 13, the time required for discharge | emission (collection | recovery) of the electrode mixture 31 can be shortened.

(4)排出部13は、タンク本体11aの底壁21に形成された開口部13aと、開口部13aの周縁からタンク本体11aの外側に突設された筒部13bとを備えている。したがって、開口部13aがタンク本体11aの側壁に形成された場合に比べて、混練されて調整された電極用合剤31を回収する際に、タンク本体11a内の全ての電極用合剤31を回収することが容易になる。また、電極用合剤31の自重を、効率良く回収に利用することができる。   (4) The discharge unit 13 includes an opening 13a formed in the bottom wall 21 of the tank main body 11a, and a cylindrical portion 13b protruding from the periphery of the opening 13a to the outside of the tank main body 11a. Therefore, compared with the case where the opening 13a is formed on the side wall of the tank main body 11a, all the electrode mixture 31 in the tank main body 11a is collected when the kneaded and adjusted electrode mixture 31 is recovered. It becomes easy to collect. Moreover, the dead weight of the electrode mixture 31 can be efficiently used for recovery.

実施形態は前記に限定されるものではなく、例えば、次のように具体化してもよい。
○ 排出部13は、タンク本体11aの底壁21に設けられる構成に限らない。例えば、図4(a),(b)に示すように、タンク本体11aの側壁22に設けられてもよい。この場合、カバー23も側壁に設けられるため、側壁22は、少なくともカバー23が設けられる部分の厚さを、カバー23を設けない場合に比べて厚くする必要がある。カバー23は平板ではなく、側壁22の曲率に対応した曲面状の板で形成される。カバー23を収容する収容部24もカバー23の形状に対応して湾曲した形状に形成される。
The embodiment is not limited to the above, and may be embodied as follows, for example.
O The discharge part 13 is not restricted to the structure provided in the bottom wall 21 of the tank main body 11a. For example, as shown to Fig.4 (a), (b), you may provide in the side wall 22 of the tank main body 11a. In this case, since the cover 23 is also provided on the side wall, it is necessary to increase the thickness of at least the portion where the cover 23 is provided compared to the case where the cover 23 is not provided. The cover 23 is not a flat plate but a curved plate corresponding to the curvature of the side wall 22. The accommodating portion 24 that accommodates the cover 23 is also formed in a curved shape corresponding to the shape of the cover 23.

○ 排出部13に設けられたフィルタ14と、混練中の原材料との接触を阻止するカバー23は必須ではなく、カバー23を設けなくてもよい。カバー23を設けない場合、排出部13を底壁21に設けても、図5に示すように、排出部13を側壁22に設けてもよい。カバー23を設けない場合、図5に示すように、フィルタ14を開口部13aの内端寄りに設けても、開口部13aの中間部に設けてもよい。   The cover 23 that prevents contact between the filter 14 provided in the discharge unit 13 and the raw material being kneaded is not essential, and the cover 23 may not be provided. When the cover 23 is not provided, the discharge part 13 may be provided on the bottom wall 21 or the discharge part 13 may be provided on the side wall 22 as shown in FIG. When the cover 23 is not provided, as shown in FIG. 5, the filter 14 may be provided near the inner end of the opening 13a or may be provided in the middle of the opening 13a.

○ 排出部13を底壁21に設ける場合、図6に示すように、開口部13aの下端が底壁21の上面と同じ高さになるように形成してもよい。この場合、電極用合剤31を回収する際に、タンク本体11a内の電極用合剤31の量が少なくなった状態でも、電極用合剤31が開口部13aを経て円滑にタンク本体11a内から排出(回収)される。   When providing the discharge part 13 in the bottom wall 21, you may form so that the lower end of the opening part 13a may become the same height as the upper surface of the bottom wall 21, as shown in FIG. In this case, even when the amount of the electrode mixture 31 in the tank body 11a is reduced when the electrode mixture 31 is recovered, the electrode mixture 31 can smoothly pass through the opening 13a in the tank body 11a. Is discharged (recovered).

○ 混練手段12を構成するブレード12aの形状は、三角枠状に限らず、適宜変更してもよい。例えば、図7に示すように、ブレード12aの形状を、タンク本体11aの底壁21と平行な部分と、その平行な部分の両端からそれぞれ垂直に上方へ延びる部分とを有する形状としてもよい。この場合、ブレード12aの形状を三角形状とした場合と異なり、混練時にブレード12aの側壁22と平行に延びる部分においてもタンク本体11aの内面とブレード12aとの間で、粉体の凝集塊を小さくする効果が得られる。   The shape of the blade 12a constituting the kneading means 12 is not limited to the triangular frame shape, and may be changed as appropriate. For example, as shown in FIG. 7, the shape of the blade 12a may be a shape having a portion parallel to the bottom wall 21 of the tank body 11a and portions extending vertically upward from both ends of the parallel portion. In this case, unlike the case where the shape of the blade 12a is triangular, the powder agglomerates are reduced between the inner surface of the tank body 11a and the blade 12a even in the portion extending parallel to the side wall 22 of the blade 12a during kneading. Effect is obtained.

○ 原材料30をタンク本体11aに投入する場合、個々の材料の粉末を別々にタンク本体11aに投入する代わりに、複数の粉末を予め溶媒なしで攪拌混合したものを投入するようにしてもよい。   In the case where the raw material 30 is put into the tank body 11a, instead of putting the powders of the individual materials into the tank body 11a separately, a mixture of a plurality of powders previously stirred without a solvent may be put in.

○ 原材料30をタンク本体11aに投入する場合、溶媒を投入した後、粉体を投入するのではなく、粉体を先に投入した後、溶媒を投入するようにしてもよい。この場合、タンク本体11aに複数の材料の粉末を投入して粉体のみで攪拌した後、溶媒を投入してもよい。または、一部の粉体、例えばバインダ、を、予め液体に混ぜた状態で、混練機に投入してもよい。   In the case where the raw material 30 is charged into the tank body 11a, the solvent may be charged after the powder is first charged instead of the powder after the solvent is charged. In this case, a plurality of powder materials may be charged into the tank body 11a and stirred with only the powder, and then the solvent may be charged. Alternatively, a part of the powder, for example, a binder, may be put into a kneader in a state of being mixed in advance with a liquid.

○ 電極用合剤31の回収時に、タンク11内を加圧ガスで加圧する場合、回収開始時から加圧を行うのではなく、回収途中から加圧を行うようにしたり、回収の終期に加圧を行うようにしたりしてもよい。   ○ When the inside of the tank 11 is pressurized with pressurized gas at the time of collecting the electrode mixture 31, pressurization is not performed from the beginning of the collection, but is performed during the collection or added at the end of the collection. You may make it perform a pressure.

○ 電極用合剤31の回収時に、加圧を行わずに回収を行うようにしてもよい。この場合、回収先がタンク本体11aより下方に存在する必要がある。
○ カバー23を遮蔽位置と退避位置とに移動させる構成は、カバー23を直線的にスライドさせる構成に代えて、カバー23を回動させる構成であってもよい。
(Circle) you may make it collect | recover without performing pressurization at the time of collection | recovery of the electrode mixture 31. FIG. In this case, the collection destination needs to exist below the tank body 11a.
The configuration for moving the cover 23 to the shielding position and the retracted position may be a configuration for rotating the cover 23 instead of the configuration for sliding the cover 23 linearly.

○ 電極用合剤としての正極用合剤の原材料は、前述した物質に限らず、適宜変更してもよい。
○ 電極用合剤として負極用合剤を調整する場合、原材料は、例えば、グラファイト等の活物質と、カルボキシセルロース(CMC)等の増粘剤と、スチレンブタジエンブロック共重合体(SBR)等のバインダとして機能し得る水に分散するポリマーと、水などの溶媒とを含む。
O The raw material of the positive electrode mixture as the electrode mixture is not limited to the substances described above, and may be appropriately changed.
○ When preparing a negative electrode mixture as an electrode mixture, raw materials include, for example, an active material such as graphite, a thickener such as carboxycellulose (CMC), and a styrene butadiene block copolymer (SBR). A polymer dispersed in water that can function as a binder and a solvent such as water are included.

○ 電極用合剤としての負極用合剤の原材料は、前述した物質に限らず、適宜変更してもよい。例えば、負極用の活物質は、リチウムイオンを吸蔵・放出し得る物質であればよい。   O The raw material of the negative electrode mixture as the electrode mixture is not limited to the substances described above, and may be appropriately changed. For example, the active material for the negative electrode may be a material that can occlude and release lithium ions.

10…混練機、11…タンク、12…混練手段、13…排出部、14…フィルタ、17…加圧口、23…カバー、30…原材料、31…電極用合剤。   DESCRIPTION OF SYMBOLS 10 ... Kneading machine, 11 ... Tank, 12 ... Kneading means, 13 ... Discharge part, 14 ... Filter, 17 ... Pressurization port, 23 ... Cover, 30 ... Raw material, 31 ... Electrode mixture.

Claims (4)

複数の原材料より混練物を製造する混練機であって、
前記原材料を収容する容器と、
前記容器内で前記原材料を混練する混練手段と、
前記容器内より混練物を排出することができる排出部と、
前記排出部に設けられたフィルタと
を備えていることを特徴とする混練機。
A kneader for producing a kneaded product from a plurality of raw materials,
A container for containing the raw materials;
Kneading means for kneading the raw materials in the container;
A discharge part capable of discharging the kneaded material from the container;
A kneading machine comprising a filter provided in the discharge unit.
前記混練物は少なくとも活物質、バインダおよび溶媒を含む電極用合剤であり、前記排出部は、前記フィルタより容器内側に配置された開閉手段を備え、前記開閉手段は、閉鎖時に、前記原材料の前記フィルタへの侵入を阻止する請求項1に記載の混練機。   The kneaded material is an electrode mixture containing at least an active material, a binder, and a solvent, and the discharge portion includes opening / closing means disposed inside the container from the filter, and the opening / closing means is configured to close the raw material when closed. The kneading machine according to claim 1 which prevents penetration to said filter. 前記容器は、前記容器の上部に、容器内へのガスの導入を可能とする供給口を備える請求項1又は請求項2に記載の混練機。   The kneading machine according to claim 1 or 2, wherein the container is provided with a supply port that enables introduction of gas into the container at an upper part of the container. 前記排出部は、容器の底部に配置されている請求項1〜請求項3のいずれか一項に記載の混練機。   The kneading machine according to any one of claims 1 to 3, wherein the discharge portion is disposed at a bottom portion of the container.
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