JP2002361152A - Double-side coater and manufacturing method of electrode for battery - Google Patents

Double-side coater and manufacturing method of electrode for battery

Info

Publication number
JP2002361152A
JP2002361152A JP2001168277A JP2001168277A JP2002361152A JP 2002361152 A JP2002361152 A JP 2002361152A JP 2001168277 A JP2001168277 A JP 2001168277A JP 2001168277 A JP2001168277 A JP 2001168277A JP 2002361152 A JP2002361152 A JP 2002361152A
Authority
JP
Japan
Prior art keywords
coating
electrode
current collector
base material
die nozzle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001168277A
Other languages
Japanese (ja)
Inventor
Naoyuki Hagiwara
直行 萩原
Kazuo Katai
一夫 片井
Seiichi Endo
精一 遠藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TDK Corp
Original Assignee
TDK Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TDK Corp filed Critical TDK Corp
Priority to JP2001168277A priority Critical patent/JP2002361152A/en
Publication of JP2002361152A publication Critical patent/JP2002361152A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Coating Apparatus (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a double-side coater for applying a coating material to the both sides of a substrate, and a manufacturing method of an electrode for a nonaqueous electrolyte battery using the double-side coater. SOLUTION: This double-side coater is provided with a traveling means for making a belt-like substrate S, of which the both sides are to be coated with the coating material, run along a fixed route, a speeder roll 11 rotating in the direction opposite to the traveling direction of the substrate S and installed on one side of the substrate S for carrying out transfer coating thereon, a means 12 for supplying the coating material to the peripheral surface of the spreader roll 11, and a die nozzle coater 13 installed on the other side of the substrate S for coating the other side of the substrate S directly.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、基材の両面に塗料
を塗布するための両面塗布装置、とりわけ電極集電体の
両面に電極合剤塗料を塗布するための両面塗布装置に関
する。また、本発明は、前記両面塗布装置を用いた非水
電解質電池用電極の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a double-side coating device for applying a coating material on both sides of a substrate, and more particularly to a double-side coating device for applying an electrode mixture coating material on both surfaces of an electrode current collector. The present invention also relates to a method for producing an electrode for a non-aqueous electrolyte battery using the double-sided coating device.

【0002】[0002]

【従来の技術】近年の各種OA機器、VTRカメラ、携
帯電話等の電子機器の小型軽量化に伴い、これら電子機
器の駆動電源として用いられる二次電池の小型軽量化や
高性能化が要求されている。このような要求に答えるべ
く、高放電電位、高放電容量の非水電解質電池としてリ
チウムイオン二次電池の開発が急速にすすめられ、実用
化されている。
2. Description of the Related Art In recent years, as electronic devices such as various OA devices, VTR cameras, and mobile phones have become smaller and lighter, secondary batteries used as drive power supplies for these electronic devices have been required to be smaller and lighter and have higher performance. ing. In order to meet such demands, development of lithium ion secondary batteries as nonaqueous electrolyte batteries with high discharge potential and high discharge capacity has been rapidly promoted and put into practical use.

【0003】非水電解質電池の正極及び負極の各電極
は、一般に、電極活物質をバインダーと混合して電極塗
料(合剤)を調製し、電極集電体の片面上に電極塗料を
塗布し、乾燥し、続いて、電極集電体の他面上に電極塗
料を塗布し、乾燥し、電極集電体の両面上に電極活物質
層を有するシート状電極を形成し、その後、シート状電
極を圧延加工し、所定の寸法に切断することにより製造
されている。
[0003] For each of the positive electrode and the negative electrode of a nonaqueous electrolyte battery, an electrode coating material (mixture) is generally prepared by mixing an electrode active material with a binder, and the electrode coating material is applied on one side of an electrode current collector. , Drying, subsequently, applying an electrode paint on the other surface of the electrode current collector, drying, forming a sheet-like electrode having an electrode active material layer on both sides of the electrode current collector, and then forming a sheet-like electrode It is manufactured by rolling an electrode and cutting it into predetermined dimensions.

【0004】ところが、片面ずつ電極塗料を逐次に塗布
し乾燥する方法では、片面を乾燥炉中で乾燥する際に、
塗布されていない集電体の他面が溶剤による影響を受け
る場合があること、塗膜の変形が起こりやすいこと、塗
布・乾燥時間がかかりコストアップの要因となること、
等の不都合がある。
[0004] However, in the method of sequentially applying and drying the electrode paint on one side at a time, when one side is dried in a drying furnace,
That the other side of the current collector that is not coated may be affected by the solvent, that the coating film is likely to be deformed, that coating and drying time is increased, and that cost is increased;
And so on.

【0005】このため、例えば、特開平8−37005
号公報には、吐出量を制御可能な定量ポンプを備えた一
対のダイヘッドコータを集電体の両面に配置して、電極
塗料を集電体両面に同時に塗布し、その後乾燥を行う方
法が記載されている。
For this reason, for example, Japanese Patent Application Laid-Open No. Hei 8-37005
The publication describes a method in which a pair of die head coaters equipped with a metering pump capable of controlling the discharge amount are arranged on both sides of the current collector, and the electrode paint is simultaneously applied to both sides of the current collector, followed by drying. Have been.

【0006】特開平11−345608号公報には、2
本の互いに逆回転する塗布ロールの間隙を塗布ロールの
回転方向と逆方向に集電体を通過させることにより、塗
布ロールのそれぞれの表面に計量機構によって一定の厚
さで供給された電極塗料を、集電体の両面に転移塗布
し、その後乾燥を行う方法が記載されている。
Japanese Patent Application Laid-Open No. H11-345608 discloses that
By passing a current collector through the gap between the application rolls rotating in opposite directions to each other in the direction opposite to the rotation direction of the application roll, the electrode paint supplied with a constant thickness by a measuring mechanism on each surface of the application roll is applied. A method is described in which transfer coating is performed on both sides of a current collector and then drying is performed.

【0007】しかしながら、両公報記載の方法では、集
電体を垂直上方に走行させながら、集電体両面に電極塗
料を塗布し乾燥を行っている。電極塗料層の厚みは乾燥
及び圧延後においても40〜400μm程度と厚く、垂
直状態での塗布では塗料の自重により均一な電極塗料層
の形成が難しい。
However, in the methods described in both publications, an electrode paint is applied to both surfaces of the current collector and dried while the current collector is running vertically upward. The thickness of the electrode paint layer is as thick as about 40 to 400 μm even after drying and rolling, and it is difficult to form a uniform electrode paint layer in a vertical application due to the weight of the paint.

【0008】[0008]

【発明が解決しようとする課題】そこで、本発明の目的
は、上記従来技術の問題点を解決し、基材の両面に塗料
を塗布するための両面塗布装置、とりわけ電極集電体の
両面に電極合剤塗料を塗布するための両面塗布装置を提
供することにある。また、本発明は、前記両面塗布装置
を用いた非水電解質電池用電極の製造方法を提供するこ
とにある。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to solve the above-mentioned problems of the prior art, and to provide a double-side coating device for applying a coating material to both surfaces of a substrate, especially to both surfaces of an electrode current collector. It is an object of the present invention to provide a double-side coating device for applying an electrode mixture paint. Another object of the present invention is to provide a method for producing an electrode for a non-aqueous electrolyte battery using the double-sided coating device.

【0009】[0009]

【課題を解決するための手段】本発明は、両面に塗料を
塗布すべき帯状基材を一定経路に沿って走行させる走行
手段と、基材の一方の面側に設けられ、基材の前記一方
の面に転写塗布を行うための、基材の走行方向とは逆方
向に回転する塗布ロールと、前記塗布ロール周面に塗料
を供給する手段と、基材の他方の面側に設けられ、基材
の前記他方の面に直接塗布を行うためのダイノズルコー
タとを備える、両面塗布装置である。この発明による両
面塗布装置では、走行させられる帯状基材の一方の面は
塗布ロールによって転写塗布され、他方の面はダイノズ
ルコータによって直接塗布される。従って、基材両面に
塗料を塗布することができる。
According to the present invention, there is provided a running means for running a strip-shaped base material to be coated with a paint on both sides along a fixed path, and a running means provided on one side of the base material, For performing transfer coating on one surface, an application roll that rotates in a direction opposite to the traveling direction of the substrate, a unit that supplies a coating material to the peripheral surface of the application roll, and provided on the other surface side of the substrate. And a die nozzle coater for directly applying the other surface of the substrate to the other surface. In the double-side coating apparatus according to the present invention, one surface of the belt-shaped substrate to be moved is transferred and coated by a coating roll, and the other surface is directly coated by a die nozzle coater. Therefore, the paint can be applied to both sides of the substrate.

【0010】本発明は、ダイノズルコータは、基材の走
行方向を基準として、基材の前記一方の面が塗布ロール
によって転写塗布される位置と同じ位置、上流側の位
置、又は下流側の位置に設けられている、前記の両面塗
布装置である。ダイノズルコータの位置とは、走行させ
られる基材に向けられたその先端吐出口の位置である。
この発明による両面塗布装置では、ダイノズルコータに
よる直接塗布の位置を、塗布ロールによる転写塗布の位
置に対して、種々変化させることができ、実施の形態に
応じて適切な位置が選択される。
According to the present invention, the die nozzle coater is preferably arranged such that, based on the traveling direction of the base material, the one surface of the base material is the same as the position where the one surface of the base material is transferred and coated by the coating roll, the upstream position, or the downstream position. The above-mentioned double-side coating device is provided at a position. The position of the die nozzle coater is the position of the leading end discharge port directed to the substrate to be run.
In the double-side coating apparatus according to the present invention, the position of the direct coating by the die nozzle coater can be variously changed with respect to the position of the transfer coating by the coating roll, and an appropriate position is selected according to the embodiment.

【0011】本発明は、ダイノズルコータは、基材の走
行方向を基準として、基材の前記一方の面が塗布ロール
によって転写塗布される位置よりも僅かだけ下流側の位
置に設けられている、前記の両面塗布装置である。この
発明による両面塗布装置では、基材の一方の面が転写塗
布され、その直後に、他方の面がダイノズルコータによ
り直接塗布される。従って、基材が孔あき基材の場合に
好適である。すなわち、基材が孔あき基材の場合には、
ダイノズルコータによる直接塗布を、塗布ロールによる
転写塗布よりも上流側の位置で行うと、直接塗布された
塗料が孔を通じて塗布ロール周面に付着してしまう不都
合がある。
In the present invention, the die nozzle coater is provided at a position slightly downstream from a position where the one surface of the base material is transferred and coated by a coating roll with reference to a running direction of the base material. , A double-sided coating device. In the double-side coating apparatus according to the present invention, one side of the substrate is transfer-coated, and immediately thereafter, the other side is directly coated by the die nozzle coater. Therefore, it is suitable when the substrate is a perforated substrate. That is, when the substrate is a perforated substrate,
If the direct application by the die nozzle coater is performed at a position upstream of the transfer application by the application roll, there is a disadvantage that the directly applied paint adheres to the peripheral surface of the application roll through the hole.

【0012】本発明は、基材が略水平状態を保って、そ
の下面が塗布ロールによって転写塗布され、上面がダイ
ノズルコータによって直接塗布され、さらに下流側に走
行させられるように、塗布ロール、ダイノズルコータ及
び走行手段が設けられている、前記の両面塗布装置であ
る。この発明による両面塗布装置では、略水平状態とさ
れた基材の両面に塗布を行う。従って、垂直状態での塗
布における塗料の自重による弊害がなく、均一な塗料層
の形成が達成される。
According to the present invention, there is provided an application roll, wherein the base material is maintained in a substantially horizontal state, the lower surface thereof is transferred and applied by an application roll, and the upper surface is directly applied by a die nozzle coater, and is further moved downstream. The above-described double-sided coating apparatus provided with a die nozzle coater and a traveling unit. In the double-sided coating apparatus according to the present invention, coating is performed on both sides of the base material which is in a substantially horizontal state. Therefore, there is no adverse effect due to the weight of the paint in the application in the vertical state, and a uniform paint layer can be formed.

【0013】本発明は、塗布ロール周面に塗料を供給す
る前記手段は、塗布ロール周面に塗料吐出ヘッドが向け
られたダイノズルである、前記の両面塗布装置である。
塗布ロール周面に塗料を供給する前記手段は、特に限定
されないが、略水平状態とされた基材の下面に転写塗布
を行うためには、ダイノズルから塗布ロール周面に塗料
を吐出させることが好適である。
[0013] The present invention is the double-sided coating apparatus described above, wherein the means for supplying the paint to the peripheral surface of the application roll is a die nozzle having a paint discharge head directed to the peripheral surface of the application roll.
The means for supplying the coating material to the peripheral surface of the application roll is not particularly limited, but in order to perform transfer coating on the lower surface of the base material in a substantially horizontal state, the coating material may be discharged from the die nozzle to the peripheral surface of the application roller. It is suitable.

【0014】本発明は、両面に塗料を塗布すべき帯状基
材を一定経路に沿って走行させ、基材の一方の面には、
基材の走行方向とは逆方向に回転する塗布ロールを介し
て塗料を転写塗布し、基材の他方の面には、ダイノズル
コータにより塗料を直接的に塗布することを含む、両面
塗布方法である。
According to the present invention, a strip-shaped base material to be coated with a paint on both sides is caused to travel along a fixed path, and one side of the base material has
A double-sided application method including transferring and applying a coating via an application roll rotating in a direction opposite to the traveling direction of the substrate, and directly applying the coating to the other surface of the substrate by a die nozzle coater. It is.

【0015】本発明は、電極活物質及びバインダーを含
む電極合剤塗料を両面に塗布すべき帯状電極集電体を一
定経路に沿って走行させ、集電体の一方の面には、集電
体の走行方向とは逆方向に回転する塗布ロールを介して
電極合剤塗料を転写塗布し、集電体の他方の面には、ダ
イノズルコータにより電極合剤塗料を直接的に塗布し、
集電体両面に電極合剤塗料層を形成し、その後、両面の
電極合剤塗料層を乾燥して、電極集電体の両面に電極活
物質層を有するシート状電極を形成することを含む、電
池用電極の製造方法である。この方法においては、塗布
ロールによる転写塗布と同時に、又は転写塗布に先立っ
て、又は転写塗布よりも後に、ダイノズルコータによる
直接塗布が行われる。
According to the present invention, a strip-shaped electrode current collector to be coated on both surfaces with an electrode mixture paint containing an electrode active material and a binder is caused to travel along a fixed path, and one side of the current collector is The electrode mixture paint is transferred and applied via an application roll rotating in the direction opposite to the running direction of the body, and the electrode mixture paint is directly applied to the other surface of the current collector by a die nozzle coater,
Forming an electrode mixture paint layer on both sides of the current collector, and then drying the electrode mixture paint layer on both sides to form a sheet-like electrode having an electrode active material layer on both sides of the electrode current collector And a method for producing a battery electrode. In this method, the direct coating is performed by a die nozzle coater at the same time as, before, or after the transfer coating by the coating roll.

【0016】本発明は、集電体が孔あき集電体又は網状
集電体であり、集電体の一方の面に塗布ロールを介して
電極合剤塗料を転写塗布し、その直後に、集電体の他方
の面にダイノズルコータにより電極合剤塗料を直接的に
塗布する、前記の電池用電極の製造方法である。
According to the present invention, the current collector is a perforated current collector or a net-like current collector, and the electrode mixture paint is transferred and applied to one surface of the current collector via a coating roll. The method for producing an electrode for a battery according to the above, wherein the electrode mixture paint is directly applied to the other surface of the current collector by a die nozzle coater.

【0017】本発明は、電極集電体を略水平状態とし
て、集電体下面に塗布ロールを介して電極合剤塗料を転
写塗布し、集電体上面にダイノズルコータにより電極合
剤塗料を直接的に塗布し、集電体両面に電極合剤塗料層
を形成し、その後、電極集電体を略水平状態で走行させ
ながら、両面の電極合剤塗料層を乾燥する、前記の電池
用電極の製造方法である。
According to the present invention, the electrode current collector is placed in a substantially horizontal state, the electrode mixture paint is transferred and applied to the lower surface of the current collector via a coating roll, and the electrode mixture paint is applied to the upper surface of the current collector by a die nozzle coater. Apply directly, form an electrode mixture paint layer on both sides of the current collector, and then dry the electrode mixture paint layer on both sides while running the electrode current collector in a substantially horizontal state. This is a method for manufacturing an electrode.

【0018】[0018]

【発明の実施の形態】本発明の両面塗布装置の実施の形
態を図面を参照して説明する。図1は、本発明の両面塗
布装置の一例の概略を示す図である。図2は、本発明の
両面塗布装置の一例の要部概略を示す図である。図3
は、本発明の両面塗布装置の他の一例の要部概略を示す
図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a double-side coating apparatus according to the present invention will be described with reference to the drawings. FIG. 1 is a view schematically showing an example of a double-sided coating apparatus according to the present invention. FIG. 2 is a view schematically showing a main part of an example of a double-sided coating apparatus according to the present invention. FIG.
FIG. 4 is a view schematically showing a main part of another example of the double-sided coating apparatus of the present invention.

【0019】図1、図2及び図3を参照して、本発明の
両面塗布装置は、巻出機(1) 、巻取機(2) 及び適宜配置
される各ガイドローラ(3)(4)(5)(6)(7)(8)から主として
構成される基材の走行手段と、塗布部と、塗布部の下流
側に配置された乾燥炉(9) とを備えている。
Referring to FIGS. 1, 2 and 3, the double-side coating apparatus of the present invention comprises an unwinding machine (1), a winding machine (2) and guide rollers (3) (4) appropriately arranged. ) (5), (6), (7), (8), a running means for the base material, which is mainly composed of a coating section, and a drying furnace (9) arranged downstream of the coating section.

【0020】塗布部は、走行させられる基材(S) の一方
の面側に設けられた塗布ロール(11)と、塗布ロール(11)
周面に塗料を供給するダイノズル(12)と、基材(S) の他
方の面側に設けられたダイノズルコータ(13)とを備え
る。
The coating section includes a coating roll (11) provided on one side of the substrate (S) to be run, and a coating roll (11).
A die nozzle (12) for supplying paint to the peripheral surface and a die nozzle coater (13) provided on the other surface side of the substrate (S) are provided.

【0021】ダイノズル(12)には、図示しない塗料供給
装置から塗料供給を受ける液溜め(12a) と、液溜め(12
a) に連通したダイスリット(12b) と、その先端吐出口
(12c)とが形成されている。ダイノズル(12)は、塗布ロ
ール(11)周面に対して先端吐出口(12c) が一定間隔を保
つように配置されている。
The die nozzle (12) has a liquid reservoir (12a) receiving a paint supply from a paint supply device (not shown) and a liquid reservoir (12a).
a) The die slit (12b) communicating with
(12c) is formed. The die nozzle (12) is arranged such that the tip discharge port (12c) keeps a constant interval with respect to the peripheral surface of the application roll (11).

【0022】ダイノズルコータ(13)には、図示しない塗
料供給装置から塗料供給を受ける液溜め(13a) と、液溜
め(13a) に連通したダイスリット(13b) と、その先端吐
出口(13c) とが形成されている。ダイノズルコータ(13)
は、走行させられる基材(S)に対して先端吐出口(13c)
が一定間隔を保つように配置されている。
The die nozzle coater (13) has a liquid reservoir (13a) that receives a paint supply from a paint supply device (not shown), a die slit (13b) communicating with the liquid reservoir (13a), and a discharge port (13c) at the tip end thereof. ) Are formed. Die nozzle coater (13)
Is a tip discharge port (13c) with respect to the substrate (S) to be run.
Are arranged at regular intervals.

【0023】塗布ロール(11)とそれよりも下流側のガイ
ドローラ(5) は、基材(S) が略水平状態を保って、その
下面が塗布ロール(11)によって転写塗布され、上面がダ
イノズルコータ(13)によって直接塗布され、さらに下流
側に走行させられるように配置されている。塗布ロール
(11)とガイドローラ(5) との間には、乾燥炉(9) が設け
られ、略水平状態を保ったまま、塗布された後の基材
(S) が乾燥されるように成されている。
The coating roll (11) and the guide roller (5) on the downstream side of the coating roll (11) keep the base material (S) in a substantially horizontal state, the lower surface thereof is transferred and coated by the coating roll (11), and the upper surface thereof is coated. It is arranged so as to be directly applied by the die nozzle coater (13) and to travel further downstream. Application roll
A drying furnace (9) is provided between (11) and the guide roller (5), and the coated base material is maintained in a substantially horizontal state.
(S) is to be dried.

【0024】図2及び図3を参照して、本発明の両面塗
布装置において、ダイノズルコータ(13)は、基材(S) の
走行方向を基準として、略水平状態とされた基材(S) 下
面が塗布ロール(11)によって転写塗布される位置と同じ
位置、上流側の位置、又は下流側の位置に、先端吐出口
(13c) が向くように設けられる。
Referring to FIG. 2 and FIG. 3, in the double-side coating apparatus of the present invention, the die nozzle coater (13) has a substantially horizontal state with respect to the traveling direction of the substrate (S). S) At the same position as the position where the lower surface is transferred and applied by the application roll (11), the upstream position, or the downstream position,
(13c) is provided to face.

【0025】図2は、ダイノズルコータ(13)の先端吐出
口(13c) が転写塗布される位置よりも距離(L1)だけ上流
側の位置に向けられた例である。あるいは、ダイノズル
コータ(13)がさらに上流側の位置に設けられてもよい。
例えば、破線で示されたAの位置、Bの位置に設けられ
てもよい。
FIG. 2 shows an example in which the tip discharge port (13c) of the die nozzle coater (13) is directed to a position upstream by a distance (L1) from a position where transfer coating is performed. Alternatively, the die nozzle coater (13) may be provided at a position further upstream.
For example, it may be provided at the position A and the position B indicated by the broken lines.

【0026】図3は、ダイノズルコータ(13)の先端吐出
口(13c) が転写塗布される位置よりも距離(L2)だけ下流
側の位置に向けられた例である。あるいは、ダイノズル
コータ(13)がさらに下流側の位置に設けられてもよい。
例えば、破線で示されたCの位置に設けられてもよい。
FIG. 3 shows an example in which the tip discharge port (13c) of the die nozzle coater (13) is directed to a position downstream by a distance (L2) from the transfer coating position. Alternatively, the die nozzle coater (13) may be provided at a position further downstream.
For example, it may be provided at a position C indicated by a broken line.

【0027】基材が通常のものであれば、ダイノズルコ
ータ(13)の配設位置は転写塗布される位置と同じ位置、
上流側の位置(図2)、又は下流側の位置(図3)のい
ずれであってもよい。ただし、ダイノズルコータ(13)
は、片面側の塗料層が湿潤状態のうちに他面側の塗布が
行われるような位置に設けられ、かつダイノズルコータ
(13)は乾燥炉(9) よりも上流側に設けられる。
If the substrate is a normal one, the arrangement position of the die nozzle coater (13) is the same as the position where transfer coating is performed,
It may be either the upstream position (FIG. 2) or the downstream position (FIG. 3). However, die nozzle coater (13)
Is provided at a position where coating on the other side is performed while the paint layer on one side is wet, and the die nozzle coater
(13) is provided upstream of the drying furnace (9).

【0028】基材が孔あき基材や網状基材の場合には、
ダイノズルコータ(13)によって直接塗布された塗料が孔
や網目を通じて塗布ロール(11)周面に付着することがな
いように、図3のように、ダイノズルコータ(13)の先端
吐出口(13c) を転写塗布される位置よりも下流側の位置
に向ける。ただし、下面側の塗料層が湿潤状態のうちに
上面側の塗布が行われるように、ダイノズルコータ(13)
は乾燥炉(9) よりも上流側に設けられる。
When the substrate is a perforated substrate or a net-like substrate,
As shown in FIG. 3, the tip outlet of the die nozzle coater (13) prevents the paint directly applied by the die nozzle coater (13) from adhering to the peripheral surface of the application roll (11) through holes or meshes. 13c) is directed to a position downstream of the position where the transfer coating is performed. However, the die nozzle coater (13) is used so that the coating on the upper side is performed while the paint layer on the lower side is wet.
Is provided upstream of the drying furnace (9).

【0029】図2における距離(L1)、図3における距離
(L2)は共に特に限定されることなく、塗布ロール(11)の
直径や塗料の粘度等に応じて任意の値を選択することが
できる。例えば、電極集電体を略水平状態として塗布を
行うためには、塗布ロール(11)直径が100mm程度の
場合、距離(L1)や距離(L2)を1〜30mm程度とすると
よい。
The distance (L1) in FIG. 2 and the distance in FIG.
(L2) is not particularly limited, and any value can be selected according to the diameter of the application roll (11), the viscosity of the coating material, and the like. For example, in order to perform the application while keeping the electrode current collector in a substantially horizontal state, when the diameter of the application roll (11) is about 100 mm, the distance (L1) and the distance (L2) may be about 1 to 30 mm.

【0030】巻回されている帯状基材(S) は巻出機(1)
から送り出され、長手方向にテンションをかけられなが
ら、基材(S) の走行方向とは逆方向に回転する塗布ロー
ル(11)周面とダイノズルコータ(13)の先端吐出口(13c)
との間を略水平状態で通過し、この際、基材(S) の両面
に塗料が塗布される。すなわち、基材(S) 下面には塗布
ロール(11)によって塗料が転写塗布され、上面にはダイ
ノズルコータ(13)の先端吐出口(13c) から吐出された塗
料が直接塗布される。両面に塗料層が形成された基材
(S) は、続いて乾燥炉(9) 中を略水平状態で通過し、そ
の後、巻取機(2)に巻き取られる。
The wound base material (S) is unwound (1)
The coating roller (11), which rotates in the direction opposite to the running direction of the substrate (S) while being tensioned in the longitudinal direction while being sent out from the base, and the discharge port (13c) at the tip of the die nozzle coater (13)
, And the coating material is applied to both sides of the substrate (S). That is, the paint is transferred and applied to the lower surface of the substrate (S) by the application roll (11), and the paint discharged from the tip outlet (13c) of the die nozzle coater (13) is directly applied to the upper surface. Base material with paint layers formed on both sides
The (S) subsequently passes through the drying furnace (9) in a substantially horizontal state, and is then wound up by a winder (2).

【0031】本発明において、略水平状態での乾燥を行
うために、特に限定されないが、次の乾燥炉を用いるこ
とが好ましい。
In the present invention, in order to carry out drying in a substantially horizontal state, there is no particular limitation, but the following drying oven is preferably used.

【0032】両面に塗布により形成された塗料層を有す
る帯状基材の両側耳端部をそれぞれ挟持する複数のクリ
ップと、クリップを基材が略水平状態を保って走行させ
られるように走行させる、基材の両側にそれぞれ配置さ
れたクリップ走行手段と、走行させられる基材上の塗料
層を乾燥させるための熱供給手段とを備える、両面塗布
体製造用乾燥炉。
A plurality of clips for sandwiching both side edges of a strip-shaped base material having a paint layer formed on both sides by coating, and running the clips so that the base material can be run while maintaining a substantially horizontal state; A drying furnace for producing a double-sided coated body, comprising: a clip running means arranged on both sides of a base material; and a heat supply means for drying a paint layer on the run base material.

【0033】クリップ走行手段は、基材走行方向の上流
側と下流側に配置された一対のスプロケットホイール
と、一対のスプロケットホイール同士の間を循環走行さ
せられる連続チェーンとを備え、連続チェーンに所定の
間隔をおいてクリップが取り付けられている、前記の両
面塗布体製造用乾燥炉。
The clip running means includes a pair of sprocket wheels arranged on the upstream side and the downstream side in the substrate running direction, and a continuous chain circulating between the pair of sprocket wheels. The drying furnace for producing a double-sided coated body described above, wherein clips are attached at intervals.

【0034】前記の乾燥炉では、乾燥されるべき塗料層
を両面に有する帯状基材は、その両側耳端部をクリップ
で挟持されて、両面の塗料層共に非接触の状態で乾燥炉
内を走行させられる。従って、両面に塗料層を有する基
材の乾燥に好適である。また、基材が略水平状態を保っ
て走行させられるので、垂直状態での乾燥における塗料
の自重による弊害がなく、均一な塗料層の形成が達成さ
れる。
In the above-mentioned drying furnace, the strip-shaped base material having the paint layer to be dried on both sides is clipped at both ear ends, and the inside of the drying furnace is kept in a state where both paint layers are not in contact with each other. You can run. Therefore, it is suitable for drying a substrate having a paint layer on both sides. Further, since the base material is allowed to travel while maintaining a substantially horizontal state, there is no adverse effect due to the weight of the paint in drying in the vertical state, and a uniform paint layer can be formed.

【0035】図4は、前記の好適な乾燥炉の一例の概略
を示す平面図である。以下の説明において、基材として
の電極集電体走行方向の上流側から下流側を見て、その
左右の側を左右というものとする。
FIG. 4 is a plan view schematically showing an example of the preferred drying furnace. In the following description, the left and right sides will be referred to as left and right when viewed from the upstream side to the downstream side in the traveling direction of the electrode current collector as the base material.

【0036】図4を参照して、好適な乾燥炉(9) は、乾
燥すべき電極合剤塗料層(Sc)が形成された帯状電極集電
体(S) の左右両側耳端部(Sl)(Sr)をそれぞれ挟持する、
左右両側にそれぞれ配列された複数のクリップ(21)(22)
と、クリップ(21)(22)を電極集電体(S) が略水平状態を
保って走行させられるように走行させる、電極集電体
(S) の左右両側にそれぞれ配置されたクリップ走行装置
(23)(24)と、図示しない熱供給装置とを備える。
Referring to FIG. 4, a preferred drying oven (9) is provided with a left and right ear end (Sl) of a strip-shaped electrode current collector (S) on which an electrode mixture paint layer (Sc) to be dried is formed. ) (Sr)
Multiple clips (21) (22) arranged on each side
And the clips (21) and (22) are moved so that the electrode current collector (S) can be run while maintaining a substantially horizontal state.
(S) Clip running devices located on both left and right sides
(23) and (24) and a heat supply device (not shown).

【0037】クリップ走行装置(23),(24) はそれぞれ、
図中の矢印で示される電極集電体走行方向の上流側と下
流側に走行方向と平行に配置された一対のスプロケット
ホイール(25)(26),(27)(28) と、一対のスプロケットホ
イール同士(25)(26),(27)(28) の間を循環走行させられ
る連続チェーン(29),(30) とを備えている。スプロケッ
トホイール(25)(26),(27)(28) は同じ高さに設置され
る。下流側に配置されたスプロケットホイール(26),(2
8) には、図示しないモータが取り付けられ、モータに
よりスプロケットホイール(26),(28) が駆動される。上
流側に配置されたスプロケットホイール(25),(27) には
連続チェーン(29),(30) の伸びや弛みを調整するための
図示しないテンショナー、例えば上流側向きにエアーシ
リンダが備えられている。連続チェーン(29),(30) に所
定の間隔をおいて複数のクリップ(21),(22) が適宜固定
部材により取り付けられている。
The clip traveling devices (23) and (24) are respectively
A pair of sprocket wheels (25), (26), (27), (28) arranged in parallel to the traveling direction on the upstream and downstream sides of the electrode current collector traveling direction indicated by arrows in the drawing, and a pair of sprockets A continuous chain (29), (30) that is circulated between wheels (25), (26), (27), (28). The sprocket wheels (25) (26), (27) (28) are installed at the same height. Sprocket wheels (26), (2
A motor (not shown) is attached to 8), and the motor drives sprocket wheels (26) and (28). The upstream sprocket wheels (25) and (27) are provided with a tensioner (not shown) for adjusting elongation and slack of the continuous chains (29) and (30), for example, an air cylinder facing upstream. I have. A plurality of clips (21) and (22) are attached to the continuous chains (29) and (30) at predetermined intervals by appropriate fixing members.

【0038】乾燥炉(9) における熱供給装置は、特に限
定されることなく、電極合剤塗料層(Sc)の乾燥温度の制
御可能な熱風供給装置を用いるとよい。熱風供給装置と
しては、例えば、乾燥炉(9) 内に、電極集電体(S) 上面
又は下面に向けられて適宜配置された熱風吹き出しノズ
ルが一般的である。ノズルは、乾燥炉(9) 外部に設けら
れたヒータ及びブロワにダクトを介して連結されてい
る。
The heat supply device in the drying furnace (9) is not particularly limited, and a hot air supply device capable of controlling the drying temperature of the electrode mixture paint layer (Sc) may be used. As the hot-air supply device, for example, a hot-air blowing nozzle appropriately arranged in the drying furnace (9) so as to face the upper or lower surface of the electrode current collector (S) is generally used. The nozzle is connected via a duct to a heater and a blower provided outside the drying furnace (9).

【0039】駆動スプロケットホイール(26),(28) の回
転により、従動スプロケットホイール(25),(27) が回転
させられると共に、連続チェーン(29),(30) はスプロケ
ットホイール同士(25)(26),(27)(28) の間を水平面内で
循環走行させられる。それにより、クリップ(21),(22)
に左右両側耳端部(Sl)(Sr)をそれぞれ挟持された帯状電
極集電体(S) は、乾燥炉(9) 内を略水平状態を保って走
行させられる。乾燥炉(9) 内を走行させられる間に、電
極集電体(S) 上面及び下面にはノズルから熱風が吹き出
され、電極合剤塗料層(Sc)が乾燥される。
The rotation of the driving sprocket wheels (26) and (28) causes the driven sprocket wheels (25) and (27) to rotate, and the continuous chains (29) and (30) cause the sprocket wheels (25) ( It can be circulated in the horizontal plane between 26), (27) and (28). As a result, the clips (21), (22)
The strip-shaped electrode current collector (S) having the left and right ear ends (Sl) and (Sr) sandwiched therebetween is run in the drying furnace (9) while maintaining a substantially horizontal state. Hot air is blown from nozzles on the upper and lower surfaces of the electrode current collector (S) while the electrode current collector (S) is running in the drying furnace (9), and the electrode mixture paint layer (Sc) is dried.

【0040】なお、乾燥炉(9) の長さ、電極集電体(S)
の走行速度、乾燥温度等は、乾燥すべき電極合剤塗料層
(Sc)の溶剤含有量、溶剤の種類、塗料層厚み等を考慮し
て、適宜定められる。
The length of the drying furnace (9), the electrode current collector (S)
The running speed, drying temperature, etc. of the electrode mixture paint layer to be dried
It is appropriately determined in consideration of the solvent content of (Sc), the type of the solvent, the thickness of the paint layer, and the like.

【0041】この乾燥炉においては、帯状電極集電体の
上下両面共に非接触状態で乾燥が行われるので、両面に
電極合剤塗料層が形成された電極集電体の乾燥に好適で
ある。さらに、電極集電体が乾燥炉内を略水平状態を保
って走行させられ乾燥が行われるので、垂直状態での乾
燥における塗料の自重による弊害がなく、上下両面の電
極合剤塗料層が同時に乾燥されるので、塗膜の変形が起
こりにくく、上下両面の均一な塗料層の形成が達成され
る。従って、この乾燥炉は、膜厚及び重さのある電極合
剤塗料層が両面に塗布された電極集電体の乾燥に非常に
好適である。
In this drying oven, since the drying is performed in a non-contact state on both the upper and lower surfaces of the strip-shaped electrode current collector, it is suitable for drying the electrode current collector having the electrode mixture paint layer formed on both surfaces. Further, since the electrode current collector is run while being kept in a substantially horizontal state in the drying furnace and drying is performed, there is no adverse effect due to the weight of the paint in drying in the vertical state, and the electrode mixture paint layers on the upper and lower surfaces are simultaneously formed. Since the coating is dried, deformation of the coating film hardly occurs, and uniform coating layers on both upper and lower surfaces are formed. Therefore, this drying oven is very suitable for drying an electrode current collector having both sides coated with an electrode mixture paint layer having a large thickness and weight.

【0042】本発明は、前記両面塗布装置を用いた非水
電解質電池用電極の製造方法にも関する。本発明の方法
においては、まず、電極活物質及びバインダーを溶剤と
共に混合することによって、スラリー状の電極合剤塗料
を調製する。この際、さらに必要に応じて導電剤や添加
剤を加えることもある。
The present invention also relates to a method for producing an electrode for a non-aqueous electrolyte battery using the double-side coating device. In the method of the present invention, first, an electrode active material and a binder are mixed with a solvent to prepare a slurry electrode mixture paint. At this time, a conductive agent or an additive may be further added as necessary.

【0043】電極活物質としては、従来より電極活物質
として使用されているものであれば特に制限なく、各種
の材料を使用することができる。正極活物質としては、
例えば、リチウムイオンをドープ・脱ドープ可能な酸化
物又は炭素材料を用いることができる。このような酸化
物としては、リチウムを含む複合酸化物が挙げられ、例
えば、コバルト酸リチウムLix CoO2 (0<x≦
1.0)、マンガン酸リチウムLi1+x Mn2-x
4 (0≦x≦1/3)、ニッケル酸リチウムLix Ni
2 (0<x≦1.0)などが挙げられる。これら酸化
物粉末の平均粒子径は1〜40μm程度が好ましい。
The electrode active material is not particularly limited as long as it has been conventionally used as an electrode active material, and various materials can be used. As the positive electrode active material,
For example, an oxide or a carbon material capable of doping / dedoping lithium ions can be used. Examples of such an oxide include a composite oxide containing lithium, for example, lithium cobalt oxide Li x CoO 2 (0 <x ≦
1.0), lithium manganate Li 1 + x Mn 2-x O
4 (0 ≦ x ≦ 1/3), lithium nickelate Li x Ni
O 2 (0 <x ≦ 1.0). The average particle size of these oxide powders is preferably about 1 to 40 μm.

【0044】負極活物質としては、例えば、炭素質材
料、リチウム金属、リチウム合金、スズ酸化物等の酸化
物が用いられる。炭素質材料としては、特に制限される
ものではなく、例えば、無定形炭素、アセチレンブラッ
ク、石油コークス、石炭コークス、人造黒鉛、天然黒
鉛、グラファイト系炭素繊維、難黒鉛化炭素等を用いる
ことができる。これらの中から、目的とする電池の特性
に応じて、当業者が適宜選択することができる。
As the negative electrode active material, for example, carbonaceous materials, lithium metals, lithium alloys, and oxides such as tin oxide are used. The carbonaceous material is not particularly limited, and examples thereof include amorphous carbon, acetylene black, petroleum coke, coal coke, artificial graphite, natural graphite, graphite-based carbon fiber, and non-graphitizable carbon. . Those skilled in the art can appropriately select from these in accordance with the characteristics of the intended battery.

【0045】電極塗料用のバインダーとしては、特に制
限されるものではなく、従来より使用されている結晶性
樹脂、非結晶性樹脂等の各種バインダーを使用すること
ができる。例えば、バインダーとして、ポリアクリルニ
トリル(PAN)、ポリエチレンテレフタレートや、ポ
リフッ化ビニリデン(PVDF) 、ポリフッ化ビニル、
フッ素ゴム等のフルオロカーボン系樹脂等を用いること
ができる。バインダーは、電極活物質100重量部に対
して、通常1〜40重量部、好ましくは2〜25重量
部、特に好ましくは5〜15重量部の量で使用される。
The binder for the electrode paint is not particularly limited, and various binders such as a crystalline resin and an amorphous resin which have been conventionally used can be used. For example, as a binder, polyacrylonitrile (PAN), polyethylene terephthalate, polyvinylidene fluoride (PVDF), polyvinyl fluoride,
A fluorocarbon-based resin such as fluororubber can be used. The binder is used in an amount of usually 1 to 40 parts by weight, preferably 2 to 25 parts by weight, particularly preferably 5 to 15 parts by weight, based on 100 parts by weight of the electrode active material.

【0046】電極塗料用の溶剤としては、特に制限され
るものではなく、電極塗料の調製する際に従来より使用
されている各種の溶剤を使用することができる。例え
ば、N−メチルピロリドン(NMP)、メチルイソブチ
ルケトン(MIBK)、メチルエチルケトン(ME
K)、シクロヘキサノン、トルエン等が挙げられる。
The solvent for the electrode paint is not particularly limited, and various solvents conventionally used for preparing the electrode paint can be used. For example, N-methylpyrrolidone (NMP), methyl isobutyl ketone (MIBK), methyl ethyl ketone (ME
K), cyclohexanone, toluene and the like.

【0047】導電剤は、必要に応じて、電極活物質の電
子伝導性を補足する目的等のため加えることができる。
導電剤としては、特に制限されるものではなく、公知の
各種導電剤を用いるとよい。例えば、アセチレンブラッ
ク、グラファイト、金・銀・銅微粒子等が挙げられる。
また、さらに炭酸リチウム、シュウ酸、マレイン酸等の
公知の各種添加剤を加えることもできる。
The conductive agent can be added, if necessary, for the purpose of supplementing the electron conductivity of the electrode active material.
The conductive agent is not particularly limited, and various known conductive agents may be used. For example, acetylene black, graphite, gold / silver / copper fine particles and the like can be mentioned.
Further, various known additives such as lithium carbonate, oxalic acid, and maleic acid can also be added.

【0048】電極活物質、バインダー、導電剤、溶剤等
の混合は、常法により行うことができる。例えば、ロー
ルミル法により、乾燥空気下や不活性ガス雰囲気下で混
合する。
The mixing of the electrode active material, the binder, the conductive agent, the solvent and the like can be performed by a conventional method. For example, mixing is performed under dry air or an inert gas atmosphere by a roll mill method.

【0049】次に、得られたスラリー状の電極塗料を、
本発明の両面塗布装置を用いて帯状電極集電体の両面に
塗布する。
Next, the obtained slurry-like electrode coating was
The two-sided coating device of the present invention is used to coat both sides of the strip-shaped electrode current collector.

【0050】本発明において、電極集電体としては、金
属箔、金属シート、パンチングメタル、金属網等が使用
され、金属箔、パンチングメタルが好適である。電極集
電体の金属材料としては、特に制限されるものではな
く、従来より電極集電体に使用されている各種の金属材
料を使用することができる。このような金属材料として
は、例えば、銅、アルミニウム、ステンレス鋼、ニッケ
ル、鉄等が挙げられ、銅、アルミニウム等が好ましい。
電極集電体の厚みは、通常1〜30μm、好ましくは5
〜20μmである。
In the present invention, as the electrode current collector, a metal foil, a metal sheet, a punched metal, a metal net, and the like are used, and a metal foil and a punched metal are preferable. The metal material of the electrode current collector is not particularly limited, and various metal materials conventionally used for the electrode current collector can be used. Examples of such a metal material include copper, aluminum, stainless steel, nickel, iron and the like, and copper, aluminum and the like are preferable.
The thickness of the electrode current collector is usually 1 to 30 μm, preferably 5 to 30 μm.
2020 μm.

【0051】電極集電体がパンチングメタル等の孔あき
集電体や金属網等の網状集電体の場合には、集電体の一
方の面に塗布ロールによる転写塗布を行った後に、他方
の面にダイノズルコータによる直接塗布を行う。
In the case where the electrode current collector is a perforated current collector such as a punching metal or a net current collector such as a metal net, one side of the current collector is subjected to transfer coating by a coating roll and then to the other side. Is directly applied by a die nozzle coater.

【0052】電極塗料の塗布に続いて、乾燥を行い、溶
剤を除去する。乾燥は、電極集電体を略水平状態で走行
させながら行うことが好ましい。略水平状態での乾燥
は、前述の好適な乾燥炉を用いて行うことができる。略
水平状態での乾燥により、集電体両面に形成された塗料
層の変形が起こることがなく、両面の塗料層の均一性を
保つことができる。例えば、30〜150℃で、5〜1
5分間程度の乾燥を行う。このようにして、電極集電体
の両面に電極活物質層が形成される。
Following application of the electrode paint, drying is performed to remove the solvent. The drying is preferably performed while the electrode current collector is running in a substantially horizontal state. Drying in a substantially horizontal state can be performed using the above-described suitable drying oven. By drying in a substantially horizontal state, the paint layers formed on both surfaces of the current collector do not deform, and the uniformity of the paint layers on both surfaces can be maintained. For example, at 30 to 150 ° C, 5 to 1
Dry for about 5 minutes. Thus, the electrode active material layers are formed on both surfaces of the electrode current collector.

【0053】乾燥後、電極活物質層が形成された電極集
電体を、ローラープレス機により圧延し、電極活物質層
の厚みを薄くし且つ一定に整え、電極体積当たりの活物
質の密度を高める。この際のプレス圧は、5〜1000
kg/cm程度である。また、電極活物質層の厚み(片
面として)は、用途にもよるが、特に限定されることな
く、40〜400μm程度である。
After drying, the electrode current collector on which the electrode active material layer is formed is rolled by a roller press to make the thickness of the electrode active material layer thin and uniform, and to reduce the density of the active material per electrode volume. Enhance. The pressing pressure at this time is 5 to 1000
It is about kg / cm. The thickness (as one side) of the electrode active material layer is not particularly limited, but is about 40 to 400 μm, depending on the use.

【0054】圧延加工の後、シート状電極を所定の寸法
に切断する。切断は、一般に、電極を製造流れ方向に沿
って所定の幅にするスリット工程と、所望の長さにする
裁断工程からなる。また、圧延加工に先立ってスリット
工程を行い、スリット工程後に圧延加工を行うこともあ
る。
After the rolling, the sheet electrode is cut into a predetermined size. The cutting generally includes a slitting step of making the electrode a predetermined width along the manufacturing flow direction, and a cutting step of making the electrode a desired length. Further, the slitting process may be performed before the rolling process, and the rolling process may be performed after the slitting process.

【0055】[0055]

【実施例】以下、実施例により本発明を更に具体的に説
明するが、本発明はこれらのみに限定されるものではな
い。 [実施例1:正極の製造]下記組成のスラリー状の正極
用塗料を調製した。
EXAMPLES The present invention will be described in more detail with reference to the following examples, but it should not be construed that the invention is limited thereto. [Example 1: Production of positive electrode] A slurry-like positive electrode coating material having the following composition was prepared.

【0056】 (正極用塗料の組成) 正極活物質:コバルト酸リチウム 100重量部 導電剤:アセチレンブラック 6.7重量部 バインダー:ポリフッ化ビニリデン(PVDF) 4.4重量部 溶剤:N−メチルピロリドン(NMP) 73重量部(Composition of Coating Material for Positive Electrode) Positive electrode active material: 100 parts by weight of lithium cobaltate Conductive agent: 6.7 parts by weight of acetylene black Binder: 4.4 parts by weight of polyvinylidene fluoride (PVDF) Solvent: N-methylpyrrolidone ( NMP) 73 parts by weight

【0057】まず、バインダー4.4重量部をNMP4
0重量部に溶解してラッカーを作製した。次に、導電剤
6.7重量部とコバルト酸リチウム粉100重量部の混
合粉に上記ラッカー44.4重量部を加えて混練し、そ
の後、混練物にNMP33重量部を加えて、正極用塗料
とした。
First, 4.4 parts by weight of the binder was added to NMP4
It was dissolved in 0 parts by weight to prepare a lacquer. Next, 44.4 parts by weight of the lacquer was added to and mixed with 6.7 parts by weight of the conductive agent and 100 parts by weight of lithium cobalt oxide powder, and then 33 parts by weight of NMP was added to the kneaded material to prepare a positive electrode coating material. And

【0058】図2を参照して、塗布ロール(11)直径10
0mm、ダイノズルコータ(13)の先端吐出口(13c) と転
写塗布される位置との距離L1を5mmとした両面塗布装
置を用いた。
Referring to FIG. 2, the application roll (11) has a diameter of 10
A double-sided coating apparatus was used in which the distance L1 between the leading end discharge port (13c) of the die nozzle coater (13) and the transfer coating position was 5 mm.

【0059】厚さ20μmのアルミニウム箔からなる帯
状電極集電体の両面に上記の正極用塗料を塗布した後、
図4に示した乾燥炉(9) で電極集電体を水平状態で6m
/分の速度で走行させながら、乾燥温度80〜130℃
で5分間乾燥して、両面に電極活物質層を形成した。乾
燥工程後の正極をローラープレス機により圧延し、片面
の電極活物質層の厚みが86μmであるシート状正極を
得た。得られた両面の活物質層の厚みは、均一であっ
た。
After coating the above positive electrode coating material on both surfaces of a 20 μm-thick strip-shaped electrode current collector made of aluminum foil,
In the drying oven (9) shown in FIG.
Drying speed of 80 to 130 ° C while running at a speed of
For 5 minutes to form electrode active material layers on both surfaces. The positive electrode after the drying step was rolled with a roller press to obtain a sheet-shaped positive electrode having a thickness of the electrode active material layer on one side of 86 μm. The thickness of the obtained active material layers on both surfaces was uniform.

【0060】[実施例2:正極の製造]図3を参照し
て、塗布ロール(11)直径40mm、ダイノズルコータ(1
3)の先端吐出口(13c) と転写塗布される位置との距離L2
を5mmとした両面塗布装置を用いた。
Example 2 Production of Positive Electrode Referring to FIG. 3, a coating roll (11) having a diameter of 40 mm and a die nozzle coater (1
The distance L2 between the tip discharge port (13c) of 3) and the transfer coating position
Was set to 5 mm.

【0061】次に、穿孔された厚さ20μmのアルミニ
ウム箔からなる孔あき帯状電極集電体(0.3mm径の
孔:開孔率50%)の両面に、実施例1で用いたのと同
じ正極用塗料を塗布した後、実施例1と同様に電極集電
体を水平状態で走行させながら、80〜130℃の乾燥
炉で乾燥して、両面に電極活物質層を形成した。連続
0.5時間の塗布を行っても、塗布ロール(11)周面に塗
料が付着することはなかった。乾燥工程後の正極をロー
ラープレス機により圧延し、片面の電極活物質層の厚み
が86μmであるシート状正極を得た。得られた両面の
活物質層の厚みは、均一であった。
Next, on both surfaces of a perforated band-shaped electrode current collector (a hole having a diameter of 0.3 mm: an opening ratio of 50%) made of a 20 μm-thick aluminum foil, the one used in Example 1 was used. After applying the same coating material for the positive electrode, the electrode current collector was dried in a drying oven at 80 to 130 ° C. while running the electrode current collector in a horizontal state, as in Example 1, to form electrode active material layers on both surfaces. The coating did not adhere to the peripheral surface of the application roll (11) even after continuous application for 0.5 hours. The positive electrode after the drying step was rolled with a roller press to obtain a sheet-shaped positive electrode having a thickness of the electrode active material layer on one side of 86 μm. The thickness of the obtained active material layers on both surfaces was uniform.

【0062】[0062]

【発明の効果】本発明の両面塗布装置によれば、効率良
く基材両面に塗料を塗布することができ、均一厚みの塗
布層を形成することができる。基材が孔あき基材であっ
ても、網状基材であっても、本発明の両面塗布装置は適
用される。
According to the double-side coating apparatus of the present invention, the coating material can be efficiently applied to both sides of the substrate, and a coating layer having a uniform thickness can be formed. The double-sided coating apparatus of the present invention is applicable whether the substrate is a perforated substrate or a mesh substrate.

【0063】特に本発明の両面塗布装置は、非水電解質
電池用電極の製造における電極塗料の塗布工程に好適に
用いられる。この両面塗布装置を用いることにより、均
一厚みの電極活物質層を一度の塗布工程で形成すること
ができる。従来の片面ずつの逐次塗布・乾燥工程に比
べ、製造工程時間の大幅短縮が達成されることは勿論で
あり、その上、均一厚みの電極活物質層が形成されるの
で、品質の安定した電極が得られる。
In particular, the double-side coating device of the present invention is suitably used in a step of applying an electrode paint in the production of an electrode for a non-aqueous electrolyte battery. By using this double-sided coating apparatus, an electrode active material layer having a uniform thickness can be formed in a single coating step. Compared with the conventional one-sided sequential application / drying process, the manufacturing process time can be significantly reduced, and the electrode active material layer having a uniform thickness is formed. Is obtained.

【0064】特に本発明の両面塗布装置は、ダイノズル
コータの位置を調整することによって、種々のタイプの
電極集電体への両面塗布に適用可能である。孔あき電極
集電体や網状電極集電体にも、簡便に両面塗布できる利
点は大きい。
In particular, the double-side coating apparatus of the present invention is applicable to double-side coating on various types of electrode current collectors by adjusting the position of a die nozzle coater. There is a great advantage that both sides can be easily applied to a perforated electrode current collector and a reticulated electrode current collector.

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

【図1】 本発明の両面塗布装置の一例の概略を示す図
である。
FIG. 1 is a view schematically showing an example of a double-sided coating apparatus according to the present invention.

【図2】 本発明の両面塗布装置の一例の要部概略を示
す図である。
FIG. 2 is a diagram schematically illustrating a main part of an example of a double-sided coating apparatus according to the present invention.

【図3】 本発明の両面塗布装置の他の一例の要部概略
を示す図である。
FIG. 3 is a view schematically showing a main part of another example of the double-sided coating apparatus of the present invention.

【図4】 本発明の好適な乾燥炉の一例の概略を示す平
面図である。
FIG. 4 is a plan view schematically showing an example of a preferred drying oven of the present invention.

【符号の説明】[Explanation of symbols]

(S) :基材 (1) :巻出機 (2) :巻取機 (3)(4)(5)(6)(7)(8):ガイドローラ (9) :乾燥炉 (11):塗布ロール (12):ダイノズル (12a) :液溜め (12b) :ダイスリット (12c) :先端吐出口 (13):ダイノズルコータ (13a) :液溜め (13b) :ダイスリット (13c) :先端吐出口 (S): Substrate (1): Unwinder (2): Winder (3) (4) (5) (6) (7) (8): Guide roller (9): Drying furnace (11) : Application roll (12): Die nozzle (12a): Liquid reservoir (12b): Die slit (12c): Tip discharge port (13): Die nozzle coater (13a): Liquid reservoir (13b): Die slit (13c): Tip outlet

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) H01M 4/04 H01M 4/04 A Z (72)発明者 遠藤 精一 東京都中央区日本橋一丁目13番1号 ティ ーディーケイ株式会社内 Fターム(参考) 4D075 AC02 AC72 AC88 AE24 DA04 DB31 DC18 EA60 4F040 AA22 AB05 AC02 4F041 AA12 AB01 4F042 AA22 DB02 DF01 5H050 AA19 BA16 CA08 CB07 CB12 DA04 EA10 EA23 GA22 GA29 HA12 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) H01M 4/04 H01M 4/04 AZ (72) Inventor Seiichi Endo 1-113 Nihonbashi, Chuo-ku, Tokyo No. 1 FDC term in TDK Corporation (reference) 4D075 AC02 AC72 AC88 AE24 DA04 DB31 DC18 EA60 4F040 AA22 AB05 AC02 4F041 AA12 AB01 4F042 AA22 DB02 DF01 5H050 AA19 BA16 CA08 CB07 CB12 DA04 EA10 EA12 GA29

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 両面に塗料を塗布すべき帯状基材を一定
経路に沿って走行させる走行手段と、 基材の一方の面側に設けられ、基材の前記一方の面に転
写塗布を行うための、基材の走行方向とは逆方向に回転
する塗布ロールと、前記塗布ロール周面に塗料を供給す
る手段と、 基材の他方の面側に設けられ、基材の前記他方の面に直
接塗布を行うためのダイノズルコータとを備える、両面
塗布装置。
1. A running means for running a strip-shaped base material to be coated with a paint on both sides along a fixed path, and provided on one surface side of the base material and performing transfer coating on said one surface of the base material. An application roll rotating in a direction opposite to the running direction of the substrate, a means for supplying a coating material to the peripheral surface of the application roll, and the other surface of the substrate provided on the other surface of the substrate. And a die nozzle coater for performing coating directly on the substrate.
【請求項2】 ダイノズルコータは、基材の走行方向を
基準として、基材の前記一方の面が塗布ロールによって
転写塗布される位置と同じ位置、上流側の位置、又は下
流側の位置に設けられている、請求項1に記載の両面塗
布装置。
2. The die nozzle coater is located at the same position, upstream position, or downstream position as the position where the one surface of the base material is transferred and coated by the coating roll with reference to the running direction of the base material. The double-sided coating device according to claim 1, which is provided.
【請求項3】 ダイノズルコータは、基材の走行方向を
基準として、基材の前記一方の面が塗布ロールによって
転写塗布される位置よりも僅かだけ下流側の位置に設け
られている、請求項1又は2に記載の両面塗布装置。
3. The die nozzle coater is provided at a position slightly downstream from a position where the one surface of the base material is transferred and coated by a coating roll with respect to a running direction of the base material. Item 3. The double-side coating device according to Item 1 or 2.
【請求項4】 基材が略水平状態を保って、その下面が
塗布ロールによって転写塗布され、上面がダイノズルコ
ータによって直接塗布され、さらに下流側に走行させら
れるように、塗布ロール、ダイノズルコータ及び走行手
段が設けられている、請求項1〜3のうちのいずれか1
項に記載の両面塗布装置。
4. An application roll and a die nozzle so that the base material is kept substantially horizontal, the lower surface is transferred and applied by an application roll, and the upper surface is directly applied by a die nozzle coater and further moved downstream. 4. The method according to claim 1, wherein a coater and a traveling means are provided.
Item 2. A double-sided coating device according to Item 1.
【請求項5】 塗布ロール周面に塗料を供給する前記手
段は、塗布ロール周面に塗料吐出ヘッドが向けられたダ
イノズルである、請求項1〜4のうちのいずれか1項に
記載の両面塗布装置。
5. The double-sided surface according to claim 1, wherein the means for supplying the coating material to the coating roll peripheral surface is a die nozzle having a coating material discharge head directed to the coating roll peripheral surface. Coating device.
【請求項6】 両面に塗料を塗布すべき帯状基材を一定
経路に沿って走行させ、 基材の一方の面には、基材の走行方向とは逆方向に回転
する塗布ロールを介して塗料を転写塗布し、基材の他方
の面には、ダイノズルコータにより塗料を直接的に塗布
することを含む、両面塗布方法。
6. A strip-shaped base material to be coated with a coating material on both sides is caused to travel along a fixed path, and one side of the base material is provided on a surface of the base material via an application roll which rotates in a direction opposite to a running direction of the base material. A double-sided coating method comprising transferring a coating material and applying the coating material directly to the other surface of the substrate by a die nozzle coater.
【請求項7】 電極活物質及びバインダーを含む電極合
剤塗料を両面に塗布すべき帯状電極集電体を一定経路に
沿って走行させ、 集電体の一方の面には、集電体の走行方向とは逆方向に
回転する塗布ロールを介して電極合剤塗料を転写塗布
し、集電体の他方の面には、ダイノズルコータにより電
極合剤塗料を直接的に塗布し、集電体両面に電極合剤塗
料層を形成し、その後、 両面の電極合剤塗料層を乾燥して、電極集電体の両面に
電極活物質層を有するシート状電極を形成することを含
む、電池用電極の製造方法。
7. A strip-shaped electrode current collector to be coated on both sides with an electrode mixture paint containing an electrode active material and a binder is caused to travel along a fixed path, and one side of the current collector is provided with a current collector. The electrode mixture paint is transferred and applied via an application roll rotating in the direction opposite to the running direction, and the electrode mixture paint is directly applied to the other surface of the current collector by a die nozzle coater, and the current is collected. A battery comprising: forming an electrode mixture paint layer on both surfaces of a body; thereafter, drying the electrode mixture paint layers on both surfaces to form a sheet-like electrode having electrode active material layers on both surfaces of an electrode current collector. Method of manufacturing electrodes.
【請求項8】 集電体が孔あき集電体又は網状集電体で
あり、集電体の一方の面に塗布ロールを介して電極合剤
塗料を転写塗布し、その直後に、集電体の他方の面にダ
イノズルコータにより電極合剤塗料を直接的に塗布す
る、請求項7に記載の電池用電極の製造方法。
8. The current collector is a perforated current collector or a net current collector, and the electrode mixture paint is transferred and applied to one surface of the current collector via an application roll. The method for producing an electrode for a battery according to claim 7, wherein the electrode mixture paint is directly applied to the other surface of the body by a die nozzle coater.
【請求項9】 電極集電体を略水平状態として、集電体
下面に塗布ロールを介して電極合剤塗料を転写塗布し、
集電体上面にダイノズルコータにより電極合剤塗料を直
接的に塗布し、集電体両面に電極合剤塗料層を形成し、
その後、 電極集電体を略水平状態で走行させながら、両面の電極
合剤塗料層を乾燥する、請求項7又は8に記載の電池用
電極の製造方法。
9. The electrode current collector is placed in a substantially horizontal state, and an electrode mixture paint is transferred and applied to the lower surface of the current collector via an application roll,
An electrode mixture paint is directly applied to the upper surface of the current collector by a die nozzle coater, and an electrode mixture paint layer is formed on both surfaces of the current collector,
The method for producing a battery electrode according to claim 7 or 8, wherein the electrode mixture paint layers on both sides are dried while the electrode current collector is running in a substantially horizontal state.
JP2001168277A 2001-06-04 2001-06-04 Double-side coater and manufacturing method of electrode for battery Pending JP2002361152A (en)

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CN103084306A (en) * 2013-01-28 2013-05-08 中银(宁波)电池有限公司 Battery steel shell inner wall graphite spraying equipment
WO2013098970A1 (en) 2011-12-27 2013-07-04 株式会社 東芝 Method for producing electrode and method for producing non-aqueous electrolyte battery
CN104511409A (en) * 2013-09-27 2015-04-15 丹阳琦瑞机械有限公司 Gluing working disc for cylindrical battery
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CN106938243A (en) * 2017-05-11 2017-07-11 河北金力新能源科技股份有限公司 A kind of horizontal type double-side high-speed coating equipment
CN111758178A (en) * 2018-02-26 2020-10-09 玛太克司马特股份有限公司 Method for manufacturing membrane electrode assembly of fuel cell
CN113471397A (en) * 2020-03-15 2021-10-01 深圳格林德能源集团有限公司 Method for increasing adhesion of lithium ion battery negative plate in coating process

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WO2013098970A1 (en) 2011-12-27 2013-07-04 株式会社 東芝 Method for producing electrode and method for producing non-aqueous electrolyte battery
CN103084306A (en) * 2013-01-28 2013-05-08 中银(宁波)电池有限公司 Battery steel shell inner wall graphite spraying equipment
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CN113471397A (en) * 2020-03-15 2021-10-01 深圳格林德能源集团有限公司 Method for increasing adhesion of lithium ion battery negative plate in coating process
CN113471397B (en) * 2020-03-15 2022-11-01 东莞格林德能源有限公司 Method for increasing adhesion of lithium ion battery negative plate in coating process

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