JP2010089460A - Method of forming layer to film - Google Patents

Method of forming layer to film Download PDF

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JP2010089460A
JP2010089460A JP2008264072A JP2008264072A JP2010089460A JP 2010089460 A JP2010089460 A JP 2010089460A JP 2008264072 A JP2008264072 A JP 2008264072A JP 2008264072 A JP2008264072 A JP 2008264072A JP 2010089460 A JP2010089460 A JP 2010089460A
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film
drum
forming
electrolyte membrane
layer
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Shiro Akiyama
史郎 秋山
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Toyota Motor Corp
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Toyota Motor Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • 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
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method of forming a layer to a film capable of enlarging a processable range for forming a film by adhering a desired material to a film without increasing a peripheral length (diameter) of a drum or a number of a drum. <P>SOLUTION: In a method of forming a film by adhering a desired material to a film while a strip band 11 is transported, the film 11 is wound around a rotating drum 12 in a spiral shape and a negative pressure is loaded on a back surface side of the drum whereby the film 11 is transported under suctioning to a surface of the drum, and the total length of the drum wound around in a spiral shape in a range of an axis direction is fallen within a range capable of adhering the desired material (a processable range), whereby the processable range can be enlarged only by increasing cycles of winding a film to the rotating drum 12. For instance, even when a layer 14 comprising 5 material-adhered layers 13 is required to form successively on the film 11, this requirement can be realized only by a film 11 is wound around the rotating drum 12 by 5 turns and adhering the desired material to the film 11 from each of 5 positions opposite against the film 11, thus forming 5 layers without increasing the peripheral length of the drum nor a number of the drum. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、帯状の膜、主に薄膜を搬送しつつその薄膜に所望の物質を付着させて層形成するための方法、特に、電解質膜を搬送しつつその電解質膜に電極触媒層を形成するための燃料電池の電極触媒層形成方法に好適する膜への層形成方法に関するものである。   The present invention relates to a method for forming a layer of a band-shaped film, mainly by transporting a thin film and attaching a desired substance to the thin film, and in particular, forming an electrode catalyst layer on the electrolyte film while transporting the electrolyte film. The present invention relates to a method for forming a layer on a membrane suitable for a method for forming an electrode catalyst layer of a fuel cell.

燃料電池の電解質膜に電極触媒層を形成する技術においては、薄膜からなる電解質膜の伸縮を避けるために、負圧を用いた電解質膜の位置保持が行われるが、従来のこのような電解質膜への電極触媒層形成技術としては特許文献1,2に記載のものがあった。
特許文献1に記載の技術は、多数の吸引孔を有する搬送ベルト上に電解質膜を載置し吸引固定しながら搬送させ、同電解質膜に電極触媒層となる溶液を塗布することで電極触媒層を形成するというものである。
しかしこの特許文献1に記載の技術では、電極触媒層となる溶液の塗布可能範囲を広げるために搬送ベルトを長くすると、電解質膜を吸引固定するための搬送ベルト裏面側における負圧状態の保持が困難となる。
また、特許文献2に記載の技術は、ドラムに掛け回され、吸着保持されて搬送される電解質膜に触媒層形成用塗工液を塗工することで電極触媒層を形成するというものであり、電解質膜の吸着保持はドラム内に負圧を発生させて行う。
この特許文献2に記載の技術における電解質膜の吸着保持も、特許文献1に記載の技術における電解質膜の吸引固定も、共に負圧を発生させて行うが、一般に、ドラム内を負圧にすることのほうが搬送ベルト裏面側を負圧にすることに比べて容易である。このことはドラムを大きくしても変わりなく、したがって、負圧を用いた電解質膜の位置保持に関しては特許文献2に記載の技術のほうが有用と考えられる。
In the technology of forming an electrode catalyst layer on an electrolyte membrane of a fuel cell, the position of the electrolyte membrane is maintained using negative pressure in order to avoid expansion and contraction of the electrolyte membrane made of a thin film. As an electrode catalyst layer forming technique, there are those described in Patent Documents 1 and 2.
The technology described in Patent Document 1 is such that an electrolyte membrane is placed on a conveyor belt having a large number of suction holes and conveyed while being sucked and fixed, and an electrode catalyst layer is applied to the electrolyte membrane by applying a solution serving as an electrode catalyst layer. Is to form.
However, in the technique described in Patent Document 1, when the conveyance belt is lengthened to widen the application range of the solution serving as the electrode catalyst layer, the negative pressure state on the back side of the conveyance belt for sucking and fixing the electrolyte membrane can be maintained. It becomes difficult.
The technique described in Patent Document 2 is to form an electrode catalyst layer by applying a coating solution for forming a catalyst layer to an electrolyte membrane that is wound around a drum, adsorbed, held, and conveyed. The adsorption holding of the electrolyte membrane is performed by generating a negative pressure in the drum.
Both the adsorption holding of the electrolyte membrane in the technique described in Patent Document 2 and the suction fixing of the electrolyte membrane in the technique described in Patent Document 1 are both performed by generating a negative pressure. This is easier than making negative pressure on the back side of the conveyor belt. This does not change even if the drum is enlarged, and therefore the technique described in Patent Document 2 is considered more useful for maintaining the position of the electrolyte membrane using negative pressure.

特開2005−38758号JP 2005-38758 A 特開2006−12525号JP 2006-12525 A

しかしながら特許文献2に記載の技術では、電極触媒層を形成するための塗工液の塗布可能範囲を広げるためにはドラムの周長を大きくするか、ドラムの数を増やさなければならないという問題点があった。
図3(a),(b)は、ドラム31の周長を大きくすることによって塗工液の塗布可能範囲(加工可能範囲)が広がる様子を示す。すなわち、ドラム31の周長を(a)図から(b)図に示すように大きくすれば矢印アに示す加工可能範囲が広がる。しかしこの方法では、図から分かるようにドラム31の直径Dを大きくしなければならず、ドラム31の占有空間増大した。例えば、ドラム31を横置きにした場合に、縦、横、両方向で寸法が増し、占有空間が増大した。なお、矢印イは電解質膜32の搬送方向を示す。
また、図示しないが、ドラムの数を増やして加工可能範囲を広げることによると、ドラム数に応じてのその占有空間が増大した。
However, in the technique described in Patent Document 2, in order to widen the application range of the coating liquid for forming the electrode catalyst layer, it is necessary to increase the circumference of the drum or increase the number of drums. was there.
FIGS. 3A and 3B show how the coating liquid application range (processable range) is widened by increasing the circumference of the drum 31. That is, if the peripheral length of the drum 31 is increased as shown in FIGS. However, in this method, the diameter D of the drum 31 has to be increased as can be seen from the figure, and the occupied space of the drum 31 is increased. For example, when the drum 31 was placed horizontally, the dimensions increased in the vertical, horizontal, and both directions, and the occupied space increased. Note that the arrow A indicates the transport direction of the electrolyte membrane 32.
Although not shown, when the number of drums is increased to expand the processable range, the occupied space corresponding to the number of drums increases.

本発明は、上記のような問題点を解消するためになされたもので、ドラムの周長(直径)を大きくしたり、ドラムの数を増やすことなく、膜に所望の物質を付着させて層形成するための加工可能範囲を広げることのできる膜への層形成方法を提供することを課題とする。   The present invention has been made in order to solve the above-described problems. A desired substance is adhered to a film without increasing the peripheral length (diameter) of the drum or increasing the number of drums. It is an object of the present invention to provide a method for forming a layer on a film that can widen the processable range for forming the film.

上記課題は、膜への層形成方法を下記各態様の構成とすることによって解決される。
各態様は、請求項と同様に、項に区分し、各項に番号を付し、必要に応じて他の項の番号を引用する形式で記載する。これは、あくまでも本発明の理解を容易にするためであり、本明細書に記載の技術的特徴及びそれらの組合わせが以下の各項に記載のものに限定されると解釈されるべきではない。また、1つの項に複数の事項が記載されている場合、それら複数の事項を常に一緒に採用しなければならないわけではなく、一部の事項のみを取り出して採用することも可能である。
The said subject is solved by setting the layer formation method to a film | membrane as the structure of each following aspect.
As with the claims, each aspect is divided into sections, each section is numbered, and is described in a form that cites the numbers of other sections as necessary. This is merely for the purpose of facilitating the understanding of the present invention, and the technical features described in this specification and combinations thereof should not be construed as being limited to those described in the following sections. . In addition, when a plurality of items are described in one section, it is not always necessary to employ the plurality of items together, and it is also possible to take out only a part of the items and employ them.

以下の各項のうち、(1)項が請求項1に、(2)項が請求項2に、(3)項が請求項3に、(5)項が請求項4に、各々対応する。(4)項は請求項に係る発明ではない。   Of the following items, (1) corresponds to claim 1, (2) corresponds to claim 2, (3) corresponds to claim 3, and (5) corresponds to claim 4. . The item (4) is not a claimed invention.

(1) 帯状の膜を搬送させつつその膜に所望の物質を付着させて層形成させる膜への層形成方法において、前記膜を、回転ドラムに螺旋状に掛け回すと共にそのドラム裏面側に負圧を生じさせてドラム表面に吸引しつつ搬送させることを特徴とする膜への層形成方法。
膜の厚みに制限はないが、いわゆる薄膜が好適する。例えば、燃料電池の電極触媒層が形成される電解質膜が適例である。膜に形成された層(付着された物質)を膜搬送中に乾燥することは応用例として望ましい。
(2) 前記膜は燃料電池の電解質膜であり、この電解質膜に付着させる物質は前記燃料電池の電極触媒層を形成させるための液状体であることを特徴とする(1)項に記載の膜への層形成方法。
本項は、(1)項に記載の膜への層形成方法を燃料電池の電極触媒層形成方法に適用した発明であり、電解質膜はイオン交換樹脂材からなり、また電極触媒層を形成するための物質は白金等からなる物質である。
(3) 前記膜を、その端面位置を定位置に制御しつつ搬送させることを特徴とする(1)項又は(2)項に記載の膜への層形成方法。
膜端面位置の定位置制御にはエッジポジションコントローラ等が用いられる。
(4) 前記膜の端面位置を、その膜の繰出し部と前記回転ドラムとの間、及び巻取り部と前記回転ドラムとの間の、各々回転ドラム近傍位置で定位置に制御することを特徴とする(3)項に記載の膜への層形成方法。
本項に記載の発明によれば、(3)項に記載の発明における螺旋角度と位置との保持をより効率的に行うことができるという効果がある。
(5) 前記回転ドラムの外周側においてそのドラムに掛け回された前記膜と対向するドラム軸方向に沿う複数箇所から、各々前記所望の物質をその膜に付着させて層形成させることを特徴とする(1)項〜(4)項のうちのいずれか1項に記載の膜への層形成方法。
(1) In a method of forming a layer on a film in which a belt-shaped film is conveyed and a desired substance is adhered to the film to form a layer, the film is spirally wound around a rotating drum and negatively charged on the back side of the drum. A method for forming a layer on a film, wherein the film is conveyed while being sucked onto the drum surface by generating pressure.
Although there is no restriction | limiting in the thickness of a film | membrane, what is called a thin film is suitable. For example, an electrolyte membrane on which an electrode catalyst layer of a fuel cell is formed is a suitable example. It is desirable as an application example to dry the layer formed on the film (attached substance) during film transportation.
(2) The membrane is an electrolyte membrane of a fuel cell, and the substance attached to the electrolyte membrane is a liquid for forming an electrode catalyst layer of the fuel cell. A method for forming a layer on a film.
This section is an invention in which the method for forming a layer on a membrane described in the section (1) is applied to a method for forming an electrode catalyst layer of a fuel cell. The electrolyte membrane is made of an ion exchange resin material and forms an electrode catalyst layer. The substance for the purpose is a substance made of platinum or the like.
(3) The method for forming a layer on a film according to (1) or (2), wherein the film is transported while controlling an end surface position thereof to a fixed position.
An edge position controller or the like is used for fixed position control of the film end face position.
(4) The position of the end face of the film is controlled to a fixed position at a position near the rotating drum, between the feeding part of the film and the rotating drum, and between the winding part and the rotating drum. The method for forming a layer on the film as described in (3).
According to the invention described in this section, there is an effect that the spiral angle and the position in the invention described in the section (3) can be held more efficiently.
(5) A layer is formed by adhering the desired substance to the film from a plurality of locations along the drum axial direction facing the film wound around the drum on the outer peripheral side of the rotating drum. The method of forming a layer on the film according to any one of (1) to (4).

(1)項に記載の発明によれば、ドラムの周長(直径)を大きくしたり、ドラムの数を増やすことなく、膜に所望の物質を付着させて層形成するための加工可能範囲を広げることのできる膜への層形成方法を提供できる。
(2)項に記載の発明によれば、燃料電池の電極触媒層を形成するための液状体の塗布可能範囲広げることのできる膜への層形成方法(燃料電池の電極触媒層形成方法)を提供できる。
(3)項に記載の発明によれば、(1)項又は(2)項に記載の膜への層形成方法において、回転ドラムに掛け回される膜の回転ドラムに対する螺旋角度と位置とを一定に保つことができる。
(5)項に記載の発明によれば、(1)項、(2)項又は(3)項に記載の膜への層形成方法において、例えば、膜上に複数層の物質からなる層の連続又は間欠形成を比較的小さなドラム占有空間で実現できる。
なお、(4)項に記載の発明は、本発明(特許請求の範囲に記載した発明)ではないの
で、上記課題を解決するための手段の欄に、その効果を述べた。
According to the invention described in the item (1), a processable range for forming a layer by attaching a desired substance to a film without increasing the peripheral length (diameter) of the drum or increasing the number of drums. A method for forming a layer on a film that can be spread can be provided.
According to the invention described in the item (2), a layer forming method (film electrode forming method for a fuel cell) on a film capable of expanding the applicable range of the liquid material for forming the electrode catalyst layer for the fuel cell is provided. Can be provided.
According to the invention described in item (3), in the method for forming a layer on a film described in item (1) or (2), the spiral angle and position of the film wound around the rotating drum with respect to the rotating drum are determined. Can be kept constant.
According to the invention described in the item (5), in the method for forming a layer on the film described in the item (1), (2) or (3), for example, a layer formed of a plurality of layers on the film is formed. Continuous or intermittent formation can be realized in a relatively small drum occupation space.
Since the invention described in the item (4) is not the present invention (the invention described in the claims), the effect is described in the column of means for solving the above problems.

以下、本発明の実施の形態を図面に基づき説明する。なお、各図間において、同一符号は同一又は相当部分を示す。
図1は、本発明による膜への層形成方法の一実施形態の説明図であって、(a)は全体図、(b)は(a)図中の回転ドラム部分を右側方から示す図である。
本実施形態は、帯状の薄膜、ここでは電解質膜を搬送させつつその電解質膜に、電極触媒層を形成するための物質を塗布させて電極触媒層を形成させる燃料電池の電極触媒層形成方法に本発明を適用したものである。この場合、電解質膜及び電極触媒層を形成するための物質は、固体高分子形燃料電池用の電極の製造に通常用いられる材料からなる。例えば、電解質膜はイオン交換樹脂材からなり、また電極触媒層を形成するための物質(電極触媒層形成物質)は白金等を含む液状体である。
Hereinafter, embodiments of the present invention will be described with reference to the drawings. In addition, the same code | symbol shows the same or an equivalent part between each figure.
FIG. 1 is an explanatory view of an embodiment of a method for forming a layer on a film according to the present invention, wherein (a) is an overall view, and (b) is a view showing a rotating drum portion in FIG. It is.
The present embodiment is a method for forming an electrode catalyst layer of a fuel cell in which a belt-shaped thin film, here an electrolyte membrane, is conveyed and a material for forming an electrode catalyst layer is applied to the electrolyte membrane to form an electrode catalyst layer. The present invention is applied. In this case, the substance for forming the electrolyte membrane and the electrode catalyst layer is made of a material usually used for manufacturing an electrode for a polymer electrolyte fuel cell. For example, the electrolyte membrane is made of an ion exchange resin material, and the substance for forming the electrode catalyst layer (electrode catalyst layer forming substance) is a liquid containing platinum or the like.

図1に示すように、本実施形態に係る燃料電池の電極触媒層形成方法は、電解質膜11を、軸周り方向に回転自在のドラム(回転ドラム)12に螺旋状に複数回、ここでは5回、掛け回すと共に、その回転ドラム12の裏面側に負圧を生じさせて上記電解質膜11を回転ドラム12表面に吸引しつつその先端側から巻き取って搬送させるものである。
この方法によれば、電解質膜11の、螺旋状に掛け回された回転ドラム軸方向の範囲ウ内における全長(電解質膜11の掛回し回数×回転ドラム周長)が電極触媒層形成物質、ここでは電極触媒層形成用液状体の塗布可能範囲(加工可能範囲)となる。したがって、加工可能範囲を広げるには、電解質膜11の回転ドラム12への掛回し回数を増やすだけですみ、ドラム周長(直径D)を大きくしたり、ドラム数を増やす必要はない。すなわち、加工可能範囲を広げることによる回転ドラム12の占有空間の増加は最小限ですむ。
As shown in FIG. 1, in the fuel cell electrode catalyst layer forming method according to the present embodiment, the electrolyte membrane 11 is spirally wound around a drum 12 (rotary drum) 12 that is rotatable in the direction around the axis a plurality of times, 5 in this case. The electrolyte membrane 11 is wound up from the front end side of the rotary drum 12 and conveyed while sucking the surface of the rotary drum 12 while generating a negative pressure on the back side of the rotary drum 12.
According to this method, the total length of the electrolyte membrane 11 in the range of the spiral drum axial direction (the number of times the electrolyte membrane 11 is wound × the circumference of the rotary drum) is the electrode catalyst layer forming substance, Then, it becomes the application possible range (processable range) of the liquid for electrode catalyst layer formation. Therefore, in order to widen the workable range, it is only necessary to increase the number of times the electrolyte membrane 11 is wound around the rotary drum 12, and it is not necessary to increase the drum peripheral length (diameter D) or increase the number of drums. That is, the increase in the space occupied by the rotating drum 12 by expanding the processable range is minimized.

本実施形態においては、上記回転ドラム12の外周側においてそのドラム12に掛け回された電解質膜11と対向する回転ドラム軸方向に沿う複数箇所、ここでは5箇所(塗布装置15a〜15e)から、各々上記電極触媒層形成用液状体を電解質膜11に付着、ここでは吹付け塗布させ、電解質膜11上に5層の電極触媒層形成用液状体塗布層13からなる電極触媒層14を形成する例を示す。   In the present embodiment, from a plurality of locations along the axial direction of the rotary drum facing the electrolyte membrane 11 wound around the drum 12 on the outer peripheral side of the rotary drum 12, here from five locations (coating devices 15a to 15e), Each of the electrode catalyst layer forming liquid materials is attached to the electrolyte membrane 11 and sprayed here, thereby forming an electrode catalyst layer 14 comprising five electrode catalyst layer forming liquid material coating layers 13 on the electrolyte membrane 11. An example is shown.

図示例において、電解質膜11は、ロール状に巻かれた状態から帯状に引き出されて上記のように回転ドラム12に螺旋状に掛け回され、回転ドラム12上における電解質膜11の塗布形成後はロール状に巻き取られる。
電解質膜11の搬送(矢印イにその方向を示す)は、電解質膜11の先端側からの巻取りにより、あるいは同巻取り及び回転ドラム12の回転駆動の併用により行われる。いずれにしても、電解質膜11が搬送中、あるいは搬送の開始、停止時において、破断しないように構成される。例えば、電解質膜11の巻取りにより電解質膜11を搬送させる場合には、回転ドラム12は軽負荷で自由回転可能に軸支され、必要に応じて適量のバックテンションが付与される。巻取り及び回転ドラム12の回転駆動の併用による場合には、電解質膜11の巻取り速度に同期するように回転ドラム12を回転させる等の構成が採られる。
In the illustrated example, the electrolyte membrane 11 is drawn out in a band shape from a state wound in a roll shape, and spirally wound around the rotary drum 12 as described above, and after the electrolyte membrane 11 is applied on the rotary drum 12, It is wound up into a roll.
The conveyance of the electrolyte membrane 11 (indicated by the direction of arrow A) is performed by winding the electrolyte membrane 11 from the distal end side or by using both the winding and the rotational drive of the rotary drum 12 in combination. In any case, the electrolyte membrane 11 is configured not to be broken during transportation or at the start or stop of transportation. For example, when the electrolyte membrane 11 is transported by winding the electrolyte membrane 11, the rotary drum 12 is pivotally supported so as to be freely rotatable with a light load, and an appropriate amount of back tension is applied as necessary. In the case of using both winding and rotational driving of the rotating drum 12, a configuration is adopted in which the rotating drum 12 is rotated so as to synchronize with the winding speed of the electrolyte membrane 11.

電解質膜11への電極触媒層形成用液状体の塗布は、回転ドラム12に掛け回された電解質膜11と対向する、ドラム軸方向に沿う5箇所に各々配置された塗布装置15(15a〜15e)によって行われる。
電極触媒層形成用液状体の塗布の形態は、電解質膜11の搬送速度(電解質膜11の巻取り速度やドラム回転速度)、搬送の開始及び停止のタイミングの制御、及び塗布装置15による電極触媒層形成用液状体塗布の開始及び停止のタイミング制御により、更にまた塗布装置15(15a〜15e)の使用台数の設定等により、種々に変えることができる

5層の電極触媒層形成用液状体塗布層を連続して形成する場合には、回転ドラム12に掛け回され搬送されている電解質膜11に対して、電解質膜11の繰出し部側の塗布装置15aから順に1台ずつ、電解質膜11の巻取り部側の塗布装置15eまで、回転ドラム12が1回転する毎に順次塗布作動を開始させ、以後塗布装置15a〜15e共に連続塗布作動させる。あるいは、始めから塗布装置15a〜15eの全ての塗布作動を開始させる。後者の、始めから塗布装置15a〜15eの全ての塗布作動を開始させる方法は、電解質膜11への電極触媒層形成用液状体の塗布層は最初から5層とはならないが、回転ドラム12の5回転以降は5層の電極触媒層形成用液状体の塗布層が連続して得られる。
5層の電極触媒層形成用液状体塗布層13からなる電極触媒層14が連続形成された電解質膜11は、その後、適宜長で裁断される。
Application of the electrode catalyst layer-forming liquid material to the electrolyte membrane 11 is performed by coating devices 15 (15a to 15e) disposed at five locations along the drum axis direction that face the electrolyte membrane 11 wound around the rotary drum 12. ).
The form of application of the electrode catalyst layer forming liquid includes the transport speed of the electrolyte membrane 11 (winding speed of the electrolyte membrane 11 and drum rotation speed), the control of the start and stop timing of transport, and the electrode catalyst by the coating device 15. Various changes can be made by controlling the timing of starting and stopping the coating of the liquid material for layer formation, and by setting the number of coating devices 15 (15a to 15e) used.
In the case where five layers of the electrode catalyst layer forming liquid material coating layer are continuously formed, the coating device on the feeding portion side of the electrolyte membrane 11 with respect to the electrolyte membrane 11 wound around the rotary drum 12 and conveyed. The coating operation is sequentially started every time the rotary drum 12 rotates one by one to the coating device 15e on the winding part side of the electrolyte membrane 11 sequentially from 15a, and thereafter the coating devices 15a to 15e are continuously coated. Alternatively, all the coating operations of the coating devices 15a to 15e are started from the beginning. The latter method of starting all the coating operations of the coating apparatuses 15a to 15e from the beginning is that the coating layer of the electrode catalyst layer forming liquid material on the electrolyte membrane 11 is not five layers from the beginning. After five rotations, five coating layers of the electrode catalyst layer forming liquid material are continuously obtained.
The electrolyte membrane 11 in which the electrode catalyst layer 14 composed of the five electrode catalyst layer forming liquid material coating layers 13 is continuously formed is then appropriately cut to a length.

塗布装置15(15a〜15e)の電極触媒層形成用液状体塗布の開始及び停止のタイミング制御によって、電解質膜11に間欠的に電極触媒層14を形成することもできる。
塗布装置15による電極触媒層形成用液状体の塗布幅の設定によれば、電極触媒層14の幅寸法を任意に設定でき、したがって、例えば電解質膜11の幅方向両端部に電極触媒層14のない部分を形成できる。
本実施形態では、電極触媒層形成用液状体はその塗布と共に乾燥も行われるが、これについては後述する。
なお、搬送中の電解質膜11は、例えばエッジポジションコントローラ16による膜端面位置の制御によって定位置に制御され、回転ドラム12に対する螺旋角度(ドラム回転軸に対する電解質膜傾斜角)と位置とを一定に保つことができる。本実施形態では、エッジポジションコントローラ16は回転ドラム12の近傍位置に配置されており、上記螺旋角度と位置との保持を効率よく行える。
The electrode catalyst layer 14 can also be intermittently formed on the electrolyte membrane 11 by controlling the start and stop timing of the application of the electrode catalyst layer forming liquid material of the coating device 15 (15a to 15e).
According to the setting of the coating width of the electrode catalyst layer forming liquid material by the coating device 15, the width dimension of the electrode catalyst layer 14 can be arbitrarily set. Therefore, for example, the electrode catalyst layer 14 is formed at both ends in the width direction of the electrolyte membrane 11. No part can be formed.
In the present embodiment, the electrode catalyst layer forming liquid is dried together with its application, which will be described later.
The electrolyte membrane 11 being transported is controlled to a fixed position, for example, by controlling the position of the film end face by the edge position controller 16, and the spiral angle with respect to the rotating drum 12 (electrolyte membrane tilt angle with respect to the drum rotation axis) and position are kept constant. Can keep. In this embodiment, the edge position controller 16 is disposed in the vicinity of the rotary drum 12 and can efficiently hold the spiral angle and position.

本実施形態では、電解質膜11の回転ドラム12表面への吸引は上記のように回転ドラム12の裏面側に負圧を生じさせて行っており、また、電極触媒層形成用液状体の乾燥はドラム表面を加温することにより行っているが、以下これらにつき、図2を参照して具体的に説明する。
図2は、電解質膜11の回転ドラム12表面への吸引及び電極触媒層形成用液状体の乾燥を説明するための図であって、(a)は図1中の回転ドラム12部分の断面構造を電解質膜11と共に一部を破断して示す図、(b)は(a)図中の回転ドラム12部分を右側方から示す図である。
図2に示すように、回転ドラム12は径方向に内,外筒12a,12bを有する二重円筒状に形成されている。
電解質膜11が掛け回される外筒12bには、ほぼ全長、全周に亘って多数の空気吸入孔21が形成され、外筒12bの右端面に設けられた排気口22に外筒12b内の空間(内筒12aとの間に形成された空間)23を通じて連通する。排気口22は図示しないポンプ等の空気吸引装置に連結されており、同空気吸引装置を作動させることにより、外筒12b裏面側、つまり回転ドラム12の裏面側に負圧が生じて空気吸入孔21から空気が吸引されるため、回転ドラム12に掛け回された電解質膜11部分を回転ドラム12表面に吸引可能である。
上記空気吸入孔21は回転ドラム12(外筒12b)に直接穿設してもよいが、回転ドラム12の外筒12bを骨組みだけで形成し、その外周を多孔体やメッシュ材で覆うことにより形成してもよい。
In the present embodiment, the suction of the electrolyte membrane 11 to the surface of the rotating drum 12 is performed by generating a negative pressure on the back side of the rotating drum 12 as described above, and the electrode catalyst layer forming liquid is dried. This is done by heating the drum surface, which will be specifically described below with reference to FIG.
FIG. 2 is a view for explaining the suction of the electrolyte membrane 11 to the surface of the rotary drum 12 and the drying of the liquid material for forming the electrode catalyst layer, wherein (a) is a cross-sectional structure of the rotary drum 12 portion in FIG. FIG. 2B is a diagram showing a part of the rotating drum 12 together with the electrolyte membrane 11, and FIG.
As shown in FIG. 2, the rotary drum 12 is formed in a double cylindrical shape having inner and outer cylinders 12a and 12b in the radial direction.
In the outer cylinder 12b around which the electrolyte membrane 11 is wound, a large number of air suction holes 21 are formed over almost the entire length, and the exhaust cylinder 22 is provided in the exhaust port 22 provided on the right end surface of the outer cylinder 12b. Communication space (space formed between the inner cylinder 12a) 23 and the inner cylinder 12a. The exhaust port 22 is connected to an air suction device such as a pump (not shown). By operating the air suction device, a negative pressure is generated on the back surface side of the outer cylinder 12b, that is, the back surface side of the rotary drum 12, and the air suction hole. Since air is sucked from 21, the portion of the electrolyte membrane 11 wound around the rotating drum 12 can be sucked to the surface of the rotating drum 12.
The air suction hole 21 may be directly drilled in the rotary drum 12 (outer cylinder 12b). However, the outer cylinder 12b of the rotary drum 12 is formed only by a framework, and the outer periphery thereof is covered with a porous body or a mesh material. It may be formed.

回転ドラム12の内筒12aには、軸方向に、ここでは軸方向の左端面から右端面に向けて(矢印オ参照)、温水を通水可能とするために、左端面には温水導入口24が右端面には排水口25が、各々通じている。そして排水口25は、図示しないポンプ等の温水循環装置に連結されており、同温水循環装置を作動させることにより、内筒12a内を左端
面から右端面に向けて温水を循環させて、内筒12a、ひいては外筒12b(回転ドラム12表面)を加熱可能である。したがって、回転ドラム12に掛け回された電解質膜11を介してその電解質膜11に塗布された電極触媒層形成用液状体を乾燥可能である。
このように、外筒12bにおける通気及び内筒12aにおける通水を各々可能とし、かつ回転ドラム全体の回転を可能とするために、Oリング26等が設けられている。
図中の矢印エは、上記負圧を生じさせるための空気流を電解質膜11が掛け回されていない状態で示す。
In the inner cylinder 12a of the rotating drum 12, in order to allow hot water to flow in the axial direction, here from the left end surface in the axial direction to the right end surface (see arrow (e)), a hot water inlet is provided on the left end surface. A drain outlet 25 communicates with each of the right end surfaces 24. The drain port 25 is connected to a hot water circulation device such as a pump (not shown), and by operating the hot water circulation device, the hot water is circulated in the inner cylinder 12a from the left end surface to the right end surface. The cylinder 12a and by extension the outer cylinder 12b (the surface of the rotating drum 12) can be heated. Therefore, the electrode catalyst layer-forming liquid material applied to the electrolyte membrane 11 can be dried through the electrolyte membrane 11 wound around the rotary drum 12.
As described above, the O-ring 26 and the like are provided in order to allow ventilation in the outer cylinder 12b and water in the inner cylinder 12a, respectively, and rotation of the entire rotating drum.
An arrow D in the figure indicates an air flow for generating the negative pressure in a state where the electrolyte membrane 11 is not wound around.

以上述べたように本実施形態では、図1に示すように、電解質膜11を、回転ドラム12に螺旋状に複数回掛け回すと共に、そのドラム裏面側に負圧を生じさせて同ドラム表面に吸引しつつその先端側から巻き取って搬送させるようにした。したがって、電解質膜11の、螺旋状に掛け回された回転ドラム軸方向の範囲ウ内における全長(電解質膜11の掛回し回数×回転ドラム周長)が電極触媒層形成用液状体の塗布可能範囲(加工可能範囲)となる。すなわち、加工可能範囲を広げるには、電解質膜11の回転ドラム12への掛回し回数を増やすだけですみ、ドラム周長(直径)を大きくしたり、ドラム数を増やす必要はない。   As described above, in the present embodiment, as shown in FIG. 1, the electrolyte membrane 11 is spirally wound around the rotating drum 12 a plurality of times, and negative pressure is generated on the back surface side of the drum so that the surface of the drum 11 is surfaced. It was taken up from the tip side while being sucked and conveyed. Therefore, the total length of the electrolyte membrane 11 in the range of the axial direction of the rotating drum that is hung around the spiral (the number of times the electrolyte membrane 11 is hung × the circumference of the rotating drum) is the range in which the electrode catalyst layer forming liquid can be applied. (Processable range). That is, in order to widen the workable range, it is only necessary to increase the number of times the electrolyte membrane 11 is wound around the rotary drum 12, and it is not necessary to increase the drum circumference (diameter) or increase the number of drums.

例えば、回転ドラム12に掛け回された電解質膜11と対向するドラム軸方向に沿う5箇所から、各々電極触媒層形成用液状体を電解質膜11に吹付け塗布させ、電解質膜11上に5層の電極触媒層形成用液状体塗布層13からなる電極触媒層14を形成したい場合に、ドラム周長を大きくしたり、ドラム数を増やすことなくその形成が可能である。
特許文献2に記載の技術においては、5層の電極触媒層形成用液状体塗布層を積層形成する場合、ドラム周方向に沿う5箇所から電極触媒層形成用液状体を吹付け塗布するか、5つのドラムを用意して各ドラムの周方向から各別に電極触媒層形成用液状体を吹付け塗布する必要がある。いずれにしても、回転ドラムの設置に必要な占有空間は可成りの大きさになるが、本実施形態によれば比較的小さな占有空間ですむ。
For example, the electrode catalyst layer forming liquid material is sprayed and applied to the electrolyte membrane 11 from five locations along the drum axial direction facing the electrolyte membrane 11 wound around the rotary drum 12, and five layers are formed on the electrolyte membrane 11. When the electrode catalyst layer 14 composed of the electrode catalyst layer forming liquid material coating layer 13 is to be formed, the electrode catalyst layer 14 can be formed without increasing the drum circumference or increasing the number of drums.
In the technique described in Patent Document 2, when five layers of the electrode catalyst layer-forming liquid material coating layer are stacked, the electrode catalyst layer-forming liquid material is sprayed and applied from five locations along the drum circumferential direction, It is necessary to prepare five drums and spray and apply the electrode catalyst layer forming liquid material from the circumferential direction of each drum. In any case, the occupied space necessary for installing the rotating drum is considerably large, but according to the present embodiment, a relatively small occupied space is sufficient.

また本実施形態では、回転ドラム12を二重円筒状に形成し、その内筒12a内に温水を通して回転ドラム12を加温するので、同ドラム12に掛け回されて搬送される電解質膜11に塗布された電極触媒層形成用液状体の乾燥をコンパクトな形態にて行うことができる。
更に、搬送中の電解質膜11については、定位置になるように制御するので、回転ドラム12に掛け回される電解質膜11の回転ドラム12に対する螺旋角度と位置とを一定に保つことができる。しかも、回転ドラム12の近傍位置で上記電解質膜11の定位置制御を行っているので、上記螺旋角度と位置との保持を効率よく行うことができる。
Further, in this embodiment, the rotary drum 12 is formed in a double cylinder shape, and the rotary drum 12 is heated through warm water in the inner cylinder 12a, so that the electrolyte membrane 11 is carried around the drum 12 and conveyed. The applied electrode catalyst layer forming liquid can be dried in a compact form.
Furthermore, since the electrolyte membrane 11 being transported is controlled to be in a fixed position, the spiral angle and position of the electrolyte membrane 11 wound around the rotary drum 12 with respect to the rotary drum 12 can be kept constant. In addition, since the position control of the electrolyte membrane 11 is performed in the vicinity of the rotating drum 12, the spiral angle and the position can be efficiently held.

なお上述実施形態では、電極触媒層形成における電極触媒層形成用液状体の乾燥を温水により行っていたが、例えば電気ヒータで行うようにしてもよい。電極触媒層形成用液状体の乾燥を行わなくてもよい。
また上述実施形態では、本発明を燃料電池の電極触媒層形成方法に適用した場合について述べたが、これのみに限定されることはない。例えば、燃料電池のガス拡散層を所定の膜に形成するためのガス拡散層形成方法に適用してもよい。
In the above-described embodiment, the electrode catalyst layer-forming liquid material in the electrode catalyst layer formation is dried with warm water. However, for example, an electrode heater may be used. The electrode catalyst layer forming liquid need not be dried.
Moreover, although the case where this invention was applied to the electrode catalyst layer formation method of a fuel cell was described in the above-mentioned embodiment, it is not limited only to this. For example, you may apply to the gas diffusion layer formation method for forming the gas diffusion layer of a fuel cell in a predetermined film | membrane.

本発明が適用された燃料電池の電極触媒層形成方法の一実施形態の説明図である。It is explanatory drawing of one Embodiment of the electrode catalyst layer formation method of the fuel cell to which this invention was applied. 同上実施形態における電解質膜のドラム表面への吸引及び電極触媒層形成用液状体の乾燥についての説明図である。It is explanatory drawing about attraction | suction to the drum surface of the electrolyte membrane in embodiment same as the above, and drying of the liquid material for electrode catalyst layer formation. 従来技術の説明図である。It is explanatory drawing of a prior art.

符号の説明Explanation of symbols

11:電解質膜、12:回転ドラム、13:電極触媒層形成用液状体塗布層、14:電極触媒層、15(15a〜15e):塗布装置、16:エッジポジションコントローラ。
DESCRIPTION OF SYMBOLS 11: Electrolyte film | membrane, 12: Rotating drum, 13: Liquid substance coating layer for electrode catalyst layer formation, 14: Electrode catalyst layer, 15 (15a-15e): Coating apparatus, 16: Edge position controller.

Claims (4)

帯状の膜を搬送させつつその膜に所望の物質を付着させて層形成させる膜への層形成方法において、
前記膜を、回転ドラムに螺旋状に掛け回すと共にそのドラム裏面側に負圧を生じさせてドラム表面に吸引しつつ搬送させることを特徴とする膜への層形成方法。
In a layer formation method to a film in which a belt-shaped film is conveyed and a desired substance is attached to the film to form a layer.
A method of forming a layer on a film, wherein the film is spirally wound around a rotating drum and negative pressure is generated on the back side of the drum so as to be conveyed while being sucked to the drum surface.
前記膜は燃料電池の電解質膜であり、この電解質膜に付着させる物質は前記燃料電池の電極触媒層を形成させるための液状体であることを特徴とする請求項1に記載の膜への層形成方法。   2. The layer on the membrane according to claim 1, wherein the membrane is an electrolyte membrane of a fuel cell, and the substance attached to the electrolyte membrane is a liquid for forming an electrode catalyst layer of the fuel cell. Forming method. 前記膜を、その端面位置を定位置に制御しつつ搬送させることを特徴とする請求項1又は2に記載の膜への層形成方法。   The method for forming a layer on a film according to claim 1 or 2, wherein the film is transported while controlling an end surface position thereof to a fixed position. 前記回転ドラムの外周側においてそのドラムに掛け回された前記膜と対向するドラム軸方向に沿う複数箇所から、各々前記所望の物質をその膜に付着させて層形成させることを特徴とする請求項1、2又は3に記載の膜への層形成方法。

The layer is formed by adhering the desired substance to the film from a plurality of locations along the drum axial direction facing the film wound around the drum on the outer peripheral side of the rotating drum. 4. A method for forming a layer on the film according to 1, 2 or 3.

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012209170A (en) * 2011-03-30 2012-10-25 Toshiba Fuel Cell Power Systems Corp Apparatus and method for manufacturing fuel cell electrode
CN114204045A (en) * 2021-10-26 2022-03-18 东风汽车集团股份有限公司 Preparation equipment and system of fuel cell membrane electrode

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012209170A (en) * 2011-03-30 2012-10-25 Toshiba Fuel Cell Power Systems Corp Apparatus and method for manufacturing fuel cell electrode
CN114204045A (en) * 2021-10-26 2022-03-18 东风汽车集团股份有限公司 Preparation equipment and system of fuel cell membrane electrode
CN114204045B (en) * 2021-10-26 2023-08-22 东风汽车集团股份有限公司 Preparation equipment and system of fuel cell membrane electrode

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