JP2007207570A - Fuel cell - Google Patents

Fuel cell Download PDF

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JP2007207570A
JP2007207570A JP2006024831A JP2006024831A JP2007207570A JP 2007207570 A JP2007207570 A JP 2007207570A JP 2006024831 A JP2006024831 A JP 2006024831A JP 2006024831 A JP2006024831 A JP 2006024831A JP 2007207570 A JP2007207570 A JP 2007207570A
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cooling medium
separator
flow path
fuel cell
oxidant gas
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JP5016228B2 (en
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Takashi Kosaka
高 小阪
Ken Takahashi
謙 高橋
Yukihiro Takeshita
享宏 竹下
Masaru Oda
優 小田
Yasuhiro Watanabe
康博 渡邊
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Honda Motor Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • 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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a fuel cell with further improved cooling efficiency, capable of easily and surely controlling flow amount of cooling media in a separator face. <P>SOLUTION: A plurality of first convex parts 44 are formed on a backside of a fuel gas flow passage 42 by arranging the fuel gas flow passage 42 on a first separator 24, and second convex parts 48 are formed on a backside of an oxidant gas flow passage 46 by arranging the oxidant gas flow passage 46 on a second separator 26. First top faces 44a of the first convex parts 44 and second top faces 48a of the second convex parts 48 constitute a continuous contact part 52 for forming separation parts 50 forming cooling media flow passages 54, and sealing areas preventing the cooling media from flowing. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、電解質の両側にアノード側電極及びカソード側電極が設けられた電解質・電極構造体と、セパレータとが積層される燃料電池に関する。   The present invention relates to a fuel cell in which an electrolyte / electrode structure in which an anode electrode and a cathode electrode are provided on both sides of an electrolyte, and a separator are laminated.

例えば、固体高分子型燃料電池は、高分子イオン交換膜からなる固体高分子電解質膜を採用している。この燃料電池は、固体高分子電解質膜の両側に、それぞれ電極触媒(電極触媒層)と多孔質カーボン(拡散層)からなるアノード側電極及びカソード側電極を配設した電解質膜・電極構造体を、セパレータ(バイポーラ板)によって挟持する発電セル(単位セル)により構成されている。通常、燃料電池では、この発電セルを所定の数だけ積層した燃料電池スタックが使用されている。   For example, a solid polymer fuel cell employs a solid polymer electrolyte membrane made of a polymer ion exchange membrane. This fuel cell has an electrolyte membrane / electrode structure in which an anode side electrode and a cathode side electrode made of an electrode catalyst (electrode catalyst layer) and porous carbon (diffusion layer) are arranged on both sides of a solid polymer electrolyte membrane, respectively. The power generation cell (unit cell) is sandwiched between separators (bipolar plates). Usually, in a fuel cell, a fuel cell stack in which a predetermined number of power generation cells are stacked is used.

上記の燃料電池では、セパレータとして、例えば、薄板状の金属プレートで構成される金属セパレータが使用される場合がある。この金属セパレータでは、プレス加工によって一方の面に反応ガス流路(燃料ガス流路又は酸化剤ガス流路)が形成されると、他方の面には、前記反応ガス流路の形状により決定された冷却媒体流路(又は他の反応ガス流路)が形成されることになる。このため、反応ガス流路の形状によっては、冷却媒体流路に沿って冷却媒体を良好に流すことができないという問題がある。   In the above fuel cell, as the separator, for example, a metal separator composed of a thin metal plate may be used. In this metal separator, when a reaction gas channel (a fuel gas channel or an oxidant gas channel) is formed on one surface by pressing, the other surface is determined by the shape of the reaction gas channel. Thus, a cooling medium flow path (or other reaction gas flow path) is formed. For this reason, there exists a problem that a cooling medium cannot be flowed favorably along a cooling medium flow path depending on the shape of the reaction gas flow path.

そこで、特許文献1に開示されている燃料電池では、電解質・電極接合体を挟持する第1及び第2セパレータは、燃料ガス及び酸化剤ガスを流通させるための中空部を有する長尺な第1及び第2中空状凸部を有し、前記第1中空状凸部と前記第2中空状凸部との頂面同士が一部離間することによって、冷却媒体を流通させる空間が形成されている。   Therefore, in the fuel cell disclosed in Patent Document 1, the first and second separators sandwiching the electrolyte / electrode assembly have long first portions having hollow portions for circulating fuel gas and oxidant gas. And the second hollow convex portion, and the top surfaces of the first hollow convex portion and the second hollow convex portion are partially separated from each other, thereby forming a space for circulating the cooling medium. .

このような構成により、互いに隣接した単位セル同士の間に、スペーサ等を使用することなく冷却水を流通させることができ、軽量且つ小型ながらも冷却効率に優れた燃料電池とすることが可能になる。   With such a configuration, cooling water can be circulated between unit cells adjacent to each other without using a spacer or the like, and a fuel cell that is lightweight and small but has excellent cooling efficiency can be obtained. Become.

特開2003−338300号公報(図4)Japanese Patent Laid-Open No. 2003-338300 (FIG. 4)

本発明はこの種の燃料電池に関するものであり、特にセパレータ面内での冷却媒体の流量制御を容易且つ確実に行うことができ、冷却効率を一層向上させることが可能な燃料電池を提供することを目的とする。   The present invention relates to a fuel cell of this type, and in particular, to provide a fuel cell capable of easily and surely controlling the flow rate of the cooling medium in the separator surface and further improving the cooling efficiency. With the goal.

本発明は、電解質の両側にアノード側電極及びカソード側電極が設けられた電解質・電極構造体と、1又は2以上のセパレータとが交互に積層される燃料電池に関するものである。   The present invention relates to a fuel cell in which an electrolyte / electrode structure in which an anode electrode and a cathode electrode are provided on both sides of an electrolyte, and one or more separators are alternately stacked.

2以上のセパレータは、積層方向に互いに重なり合う第1及び第2セパレータを有し、前記第1セパレータは、アノード側電極に供給される燃料ガスを流通させる複数の燃料ガス流路用第1凹部を設けるとともに、前記第1凹部の裏面側には、長尺な屈曲乃至湾曲する第1凸状部が形成されている。第2セパレータは、カソード側電極に供給される酸化剤ガスを流通させる複数の酸化剤ガス流路用第2凹部を設けるとともに、前記第2凹部の裏面側には、第1凸状部に対向し且つ該第1凸状部と同一方向に延在する長尺な屈曲乃至湾曲する第2凸状部が形成されている。   The two or more separators have first and second separators that overlap each other in the stacking direction, and the first separator has a plurality of first recesses for fuel gas passages through which the fuel gas supplied to the anode-side electrode flows. A long convex or curved first convex part is formed on the back side of the first concave part. The second separator is provided with a plurality of second oxidant gas channel recesses for circulating the oxidant gas supplied to the cathode side electrode, and is opposed to the first convex part on the back surface side of the second recesses. In addition, a long, bent or curved second convex portion extending in the same direction as the first convex portion is formed.

そして、第1凸状部の第1頂面と第2凸状部の第2頂面とは、互いに離間してセパレータ面方向に冷却媒体を流通させる冷却媒体流路を設けるための離間部と、所定の長さにわたって互いに積層方向に接触し、前記冷却媒体流路の流れ方向に沿う前記冷却媒体の流通を阻止する封止領域を形成するための連続接触部とを構成している。   And the 1st top surface of the 1st convex part and the 2nd top surface of the 2nd convex part are separated from each other, and a separation part for providing a cooling medium channel which distributes a cooling medium in the separator surface direction And a continuous contact portion for forming a sealing region that contacts with each other over a predetermined length in the stacking direction and prevents the flow of the cooling medium along the flow direction of the cooling medium flow path.

また、第1及び第2凸状部は、連続して異なる方向に交互に屈曲する第1及び第2屈曲部を有し、離間部では、前記第1及び第2屈曲部の振幅と長さとが同一で且つ位相が相違するとともに、連続接触部では、前記第1及び第2屈曲部の位相が一致することが好ましい。   The first and second convex portions have first and second bent portions that are alternately bent in different directions in succession, and in the separation portion, the amplitude and length of the first and second bent portions are set. Are the same and have different phases, and in the continuous contact portion, the phases of the first and second bent portions preferably match.

本発明によれば、冷却媒体流路内には、連続接触部を介して冷却媒体の流通を阻止する封止領域が形成されるため、前記冷却媒体流路は、実質的に、複数の流路部に分割される。従って、例えば、冷却媒体流路内の特定流路部の流量のみを変更することができる。これにより、セパレータ面内における冷却媒体の流量制御が容易且つ確実に遂行され、前記セパレータ面内での温度分布が良好に制御されるとともに、冷却効率を一層向上させることが可能になる。   According to the present invention, the cooling medium flow path is formed with a plurality of flow paths substantially because the cooling medium flow path is formed with a sealing region that prevents the flow of the cooling medium through the continuous contact portion. Divided into road sections. Therefore, for example, only the flow rate of the specific flow path portion in the cooling medium flow path can be changed. Thereby, the flow control of the cooling medium in the separator surface can be easily and reliably performed, the temperature distribution in the separator surface can be controlled well, and the cooling efficiency can be further improved.

図1は、本発明の実施形態に係る燃料電池10の概略斜視説明図であり、図2は、前記燃料電池10を構成する発電セル12の要部分解斜視図である。   FIG. 1 is a schematic perspective view of a fuel cell 10 according to an embodiment of the present invention, and FIG. 2 is an exploded perspective view of a main part of a power generation cell 12 constituting the fuel cell 10.

燃料電池10は、複数の発電セル12を矢印A方向に積層した積層体14を備える。積層体14の積層方向両端には、ターミナルプレート16a、16b、絶縁プレート18a、18b及びエンドプレート20a、20bが配設されており、前記エンドプレート20a、20b間には、所定の締め付け荷重が付与されている。なお、燃料電池10は、積層体14を図示しない箱状のケーシング内に収容して構成してもよい。   The fuel cell 10 includes a stacked body 14 in which a plurality of power generation cells 12 are stacked in the direction of arrow A. Terminal plates 16a and 16b, insulating plates 18a and 18b, and end plates 20a and 20b are disposed at both ends in the stacking direction of the laminate 14, and a predetermined tightening load is applied between the end plates 20a and 20b. Has been. The fuel cell 10 may be configured by housing the laminate 14 in a box-shaped casing (not shown).

図2に示すように、発電セル12は、電解質膜(電解質)・電極構造体22と、前記電解質膜・電極構造体22を挟持する第1及び第2セパレータ24、26とを備える。第1及び第2セパレータ24、26は、縦長の金属製プレートで構成されている。   As shown in FIG. 2, the power generation cell 12 includes an electrolyte membrane (electrolyte) / electrode structure 22, and first and second separators 24 and 26 that sandwich the electrolyte membrane / electrode structure 22. The 1st and 2nd separators 24 and 26 are comprised by the vertically long metal plate.

発電セル12の矢印C方向の一端縁部(上端縁部)には、積層方向である矢印A方向に互いに連通して、酸化剤ガス、例えば、酸素含有ガスを供給するための酸化剤ガス供給連通孔30a、及び燃料ガスを供給するための燃料ガス供給連通孔32aが、矢印B方向に配列して設けられる。   An oxidant gas supply for supplying an oxidant gas, for example, an oxygen-containing gas, communicates with one end edge (upper edge) in the arrow C direction of the power generation cell 12 in the arrow A direction which is the stacking direction. A communication hole 30a and a fuel gas supply communication hole 32a for supplying fuel gas are arranged in the direction of arrow B.

発電セル12の矢印C方向の他端縁部(下端縁部)には、積層方向である矢印A方向に互いに連通して、酸化剤ガスを排出するための酸化剤ガス排出連通孔30b、及び燃料ガスを排出するための燃料ガス排出連通孔32bが、矢印B方向に配列して設けられる。   The other end edge (lower end edge) of the power generation cell 12 in the direction of arrow C communicates with each other in the direction of arrow A, which is the stacking direction, and an oxidant gas discharge communication hole 30b for discharging oxidant gas, and Fuel gas discharge communication holes 32b for discharging the fuel gas are arranged in the direction of arrow B.

発電セル12の矢印B方向の一端縁部には、積層方向である矢印A方向に互いに連通して、冷却媒体を供給するための4つの冷却媒体供給連通孔34aが矢印C方向に配列して設けられる。発電セル12の矢印B方向の他端縁部には、積層方向である矢印A方向に互いに連通して、冷却媒体を排出するための4つの冷却媒体排出連通孔34bが矢印C方向に配列して設けられる。   At one end edge of the power generation cell 12 in the arrow B direction, four cooling medium supply communication holes 34a are arranged in the arrow C direction so as to communicate with each other in the direction of arrow A, which is the stacking direction. Provided. At the other end edge of the power generation cell 12 in the arrow B direction, four cooling medium discharge communication holes 34b are arranged in the arrow C direction so as to communicate with each other in the direction of arrow A, which is the stacking direction. Provided.

電解質膜・電極構造体22は、例えば、パーフルオロスルホン酸の薄膜に水が含浸された固体高分子電解質膜36と、該固体高分子電解質膜36を挟持するアノード側電極38及びカソード側電極40とを備える。   The electrolyte membrane / electrode structure 22 includes, for example, a solid polymer electrolyte membrane 36 in which a perfluorosulfonic acid thin film is impregnated with water, and an anode side electrode 38 and a cathode side electrode 40 that sandwich the solid polymer electrolyte membrane 36. With.

アノード側電極38及びカソード側電極40は、カーボンペーパ等からなるガス拡散層(図示せず)と、白金合金が表面に担持された多孔質カーボン粒子が前記ガス拡散層の表面に一様に塗布して形成される電極触媒層(図示せず)とを有する。電極触媒層は、固体高分子電解質膜36の両面に形成される。   The anode side electrode 38 and the cathode side electrode 40 are uniformly coated on the surface of the gas diffusion layer with a gas diffusion layer (not shown) made of carbon paper or the like and porous carbon particles carrying a platinum alloy on the surface. An electrode catalyst layer (not shown). The electrode catalyst layers are formed on both surfaces of the solid polymer electrolyte membrane 36.

図3に示すように、第1セパレータ24の電解質膜・電極構造体22側の面24aには、燃料ガス供給連通孔32aと燃料ガス排出連通孔32bとに連通する燃料ガス流路42が形成される。   As shown in FIG. 3, a fuel gas flow path 42 communicating with the fuel gas supply communication hole 32a and the fuel gas discharge communication hole 32b is formed on the surface 24a of the first separator 24 on the electrolyte membrane / electrode structure 22 side. Is done.

燃料ガス流路42は、左右に交互に屈曲して、すなわち、ジグザグに矢印C方向に蛇行して延在する複数の燃料ガス流路溝(第1凹部)42aを有する。燃料ガス流路42の裏面側には、すなわち、第1セパレータ24の面24b側には、各燃料ガス流路溝42aを設けることによって、前記面24b側に突出する長尺な屈曲(又は湾曲)する第1凸状部44が形成される(図2参照)。図4に示すように、各第1凸状部44の第1頂面44aは、ジグザグに形成されるとともに、第1セパレータ24の面24bと平行にして設けられる。各第1頂面44aは、一方の山部間が全て長さH1に設定される。   The fuel gas channel 42 has a plurality of fuel gas channel grooves (first recesses) 42a that are alternately bent to the left and right, that is, zigzag and meander in the direction of the arrow C. By providing each fuel gas flow channel groove 42a on the back surface side of the fuel gas flow channel 42, that is, on the surface 24b side of the first separator 24, a long bend (or curve) protruding toward the surface 24b side is provided. ) Are formed (see FIG. 2). As shown in FIG. 4, the first top surface 44 a of each first convex portion 44 is formed in a zigzag manner and is provided in parallel with the surface 24 b of the first separator 24. Each of the first top surfaces 44a is set to have a length H1 between the one crests.

図2に示すように、第2セパレータ26の電解質膜・電極構造体22側の面26aには、酸化剤ガス供給連通孔30aと酸化剤ガス排出連通孔30bとに連通する酸化剤ガス流路46が形成される。酸化剤ガス流路46は、左右に交互に屈曲して、すなわち、ジグザグに矢印C方向に延在する蛇行流路である複数の酸化剤ガス流路溝(第2凹部)46aを有する。   As shown in FIG. 2, an oxidant gas flow path communicating with the oxidant gas supply communication hole 30a and the oxidant gas discharge communication hole 30b is formed on the surface 26a of the second separator 26 on the electrolyte membrane / electrode structure 22 side. 46 is formed. The oxidant gas flow path 46 has a plurality of oxidant gas flow path grooves (second recesses) 46a that are alternately bent left and right, that is, meandering flow paths zigzag extending in the direction of arrow C.

各酸化剤ガス流路溝46aの裏面側には、すなわち、図5に示すように、第2セパレータ26の面26b側には、矢印C方向に長尺な屈曲(又は湾曲)する第2凸状部48が形成される。第2凸状部48の第2頂面48aは、第2セパレータ26の面26bから突出し且つこの面26aに平行に形成される(図4参照)。   On the back surface side of each oxidant gas flow channel groove 46a, that is, as shown in FIG. 5, on the surface 26b side of the second separator 26, a second protrusion that is bent (or curved) long in the direction of arrow C. A shaped portion 48 is formed. The second top surface 48a of the second convex portion 48 protrudes from the surface 26b of the second separator 26 and is formed parallel to the surface 26a (see FIG. 4).

各第2頂面48aは、矢印C方向に向かって左右方向(矢印A方向)に交互に屈曲するとともに、一方の山部間には、長さH1を有する領域と、長さH2(=2×H1)を有する領域とが設けられる。長さH1を有する領域は、矢印A方向に沿って冷却媒体供給連通孔34a及び冷却媒体排出連通孔34bの開口幅寸法に対応する一方、長さH2を有する領域は、前記冷却媒体供給連通孔34a間及び前記冷却媒体排出連通孔34b間に対応している。   Each second top surface 48a is alternately bent in the left-right direction (arrow A direction) in the direction of arrow C, and a region having a length H1 and a length H2 (= 2) between one peak. A region having xH1). The region having the length H1 corresponds to the opening width dimension of the cooling medium supply communication hole 34a and the cooling medium discharge communication hole 34b along the arrow A direction, while the region having the length H2 is the cooling medium supply communication hole. 34a and between the cooling medium discharge communication holes 34b.

第2頂面48aの長さH1に対応する領域では、前記第2頂面48aの振幅及び長さH1が第1凸状部44の第1頂面44aの振幅及び長さH1と同一で且つ位相が反転しており、離間部50を構成する。第2頂面48aの長さH2を有する領域では、第1頂面44aの位相と一致して互いに接触しており、連続接触部52を構成する。   In the region corresponding to the length H1 of the second top surface 48a, the amplitude and length H1 of the second top surface 48a are the same as the amplitude and length H1 of the first top surface 44a of the first convex portion 44, and The phase is reversed, and the separation portion 50 is formed. In the region having the length H <b> 2 of the second top surface 48 a, the phases of the first top surface 44 a coincide with each other and are in contact with each other, and constitute a continuous contact portion 52.

第1セパレータ24の面24a、24bには、この第1セパレータ24の外周端縁部を周回して第1シール部材53aが一体成形される。第2セパレータ26の面26a、26bには、この第2セパレータ26の外周端縁部を周回して第2シール部材53bが一体成形される。   A first seal member 53 a is integrally formed on the surfaces 24 a and 24 b of the first separator 24 around the outer peripheral edge of the first separator 24. A second seal member 53 b is integrally formed on the surfaces 26 a and 26 b of the second separator 26 so as to go around the outer peripheral edge of the second separator 26.

そこで、一方の発電セル12を構成する第1セパレータ24と、他方の発電セル12を構成する第2セパレータ26とは、互いに重なり合うことにより、第1及び第2凸状部44、48の第1及び第2頂面44a、48aが互いに離間して、すなわち、離間部50が設けられる。この離間部50に対応して、セパレータ面方向に冷却媒体を流通させる冷却媒体流路54が設けられる。   Therefore, the first separator 24 constituting the one power generation cell 12 and the second separator 26 constituting the other power generation cell 12 are overlapped with each other, so that the first and second convex portions 44 and 48 are first. The second top surfaces 44a and 48a are spaced apart from each other, that is, a spacing portion 50 is provided. Corresponding to the separation portion 50, a cooling medium flow path 54 for circulating the cooling medium in the separator surface direction is provided.

また、第1及び第2頂面44a、48a同士が所定の長さにわたって互いに積層方向に接触する領域、すなわち、連続接触部52が設けられる。この連続接触部52では、冷却媒体流路54の流れ方向に沿う冷却媒体の流通を阻止する封止領域が構成される。   Moreover, the area | region where the 1st and 2nd top surfaces 44a and 48a mutually contact in a lamination direction over predetermined length, ie, the continuous contact part 52, is provided. In the continuous contact portion 52, a sealing region that prevents the flow of the cooling medium along the flow direction of the cooling medium flow path 54 is configured.

このように構成される燃料電池10の動作について、以下に説明する。   The operation of the fuel cell 10 configured as described above will be described below.

燃料電池10内には、空気等の酸素含有ガスである酸化剤ガス、水素含有ガス等の燃料ガス、及び純水やエチレングリコール等の冷却媒体が供給される。このため、図2に示すように、酸化剤ガス供給連通孔30aから第2セパレータ26の酸化剤ガス流路46に酸化剤ガスが導入され、この酸化剤ガスが各酸化剤ガス流路溝46aをジグザグに流れることにより、電解質膜・電極構造体22を構成するカソード側電極40に沿って鉛直下方向に移動する。   The fuel cell 10 is supplied with an oxidant gas that is an oxygen-containing gas such as air, a fuel gas such as a hydrogen-containing gas, and a cooling medium such as pure water or ethylene glycol. For this reason, as shown in FIG. 2, an oxidant gas is introduced into the oxidant gas flow path 46 of the second separator 26 from the oxidant gas supply communication hole 30a, and this oxidant gas flows into each oxidant gas flow path groove 46a. Is moved in a vertical downward direction along the cathode side electrode 40 constituting the electrolyte membrane / electrode structure 22.

一方、燃料ガスは、燃料ガス供給連通孔32aから第1セパレータ24の燃料ガス流路42に導入される。図3に示すように、燃料ガスは、各燃料ガス流路溝42aをジグザグに流れることにより、電解質膜・電極構造体22を構成するアノード側電極38に沿って鉛直下方向に移動する。従って、電解質膜・電極構造体22では、カソード側電極40に供給される酸化剤ガスと、アノード側電極38に供給される燃料ガスとが、電極触媒層内で電気化学反応により消費され、発電が行われる。   On the other hand, the fuel gas is introduced into the fuel gas flow path 42 of the first separator 24 from the fuel gas supply communication hole 32a. As shown in FIG. 3, the fuel gas moves in a vertically downward direction along the anode-side electrode 38 constituting the electrolyte membrane / electrode structure 22 by flowing in zigzags through each fuel gas flow channel groove 42 a. Therefore, in the electrolyte membrane / electrode structure 22, the oxidant gas supplied to the cathode side electrode 40 and the fuel gas supplied to the anode side electrode 38 are consumed by an electrochemical reaction in the electrode catalyst layer, thereby generating power. Is done.

カソード側電極40に供給されて消費された酸化剤ガスは、酸化剤ガス排出連通孔30bに沿って矢印A方向に排出される。同様に、アノード側電極38に供給されて消費された燃料ガスは、燃料ガス排出連通孔32bに沿って矢印A方向に排出される。   The oxidant gas consumed by being supplied to the cathode side electrode 40 is discharged in the direction of arrow A along the oxidant gas discharge communication hole 30b. Similarly, the fuel gas consumed by being supplied to the anode electrode 38 is discharged in the direction of arrow A along the fuel gas discharge communication hole 32b.

また、冷却媒体供給連通孔34aに供給された冷却媒体は、第1及び第2セパレータ24、26間の冷却媒体流路54に導入された後、矢印B方向に沿って流通する。この冷却媒体は、電解質膜・電極構造体22を冷却した後、冷却媒体排出連通孔34bから排出される。   The cooling medium supplied to the cooling medium supply communication hole 34a is introduced into the cooling medium flow path 54 between the first and second separators 24 and 26 and then circulates in the direction of arrow B. This cooling medium is discharged from the cooling medium discharge communication hole 34b after the electrolyte membrane / electrode structure 22 is cooled.

この場合、本実施形態では、図4に示すように、第1凸状部44の第1頂面44aと第2凸状部48の第2頂面48aとは、離間部50に対応して互いに位相を反転させることにより、セパレータ面方向に冷却媒体を流通させる冷却媒体流路54が設けられている。   In this case, in this embodiment, as shown in FIG. 4, the first top surface 44 a of the first convex portion 44 and the second top surface 48 a of the second convex portion 48 correspond to the spacing portion 50. A cooling medium flow path 54 is provided for circulating the cooling medium in the separator surface direction by reversing the phases.

一方、各冷却媒体供給連通孔34a間及び各冷却媒体排出連通孔34b間には、第1及び第2頂面44a、48aが所定の長さH2にわたって互いに積層方向に接触し、連続接触部52を設けている。このため、冷却媒体流路54は、実質的に4つの冷却媒体流路部54a、54b、54c及び54dに分割されている。   On the other hand, between the cooling medium supply communication holes 34a and between the cooling medium discharge communication holes 34b, the first and second top surfaces 44a and 48a contact each other in the stacking direction over a predetermined length H2, and the continuous contact portion 52 Is provided. For this reason, the cooling medium flow path 54 is substantially divided into four cooling medium flow path portions 54a, 54b, 54c and 54d.

従って、冷却媒体流路54内の特定流路部、例えば、冷却媒体流路部54aの流量を、他の冷却媒体流路部54b〜54dの流量よりも多く設定することができ、特に発熱が著しい酸化剤ガス供給連通孔30a及び燃料ガス供給連通孔32aの近傍を効果的に冷却することが可能になる。これにより、セパレータ面内における冷却媒体の流量制御が容易且つ確実に遂行され、前記セパレータ面内での温度分布が良好に制御されるとともに、冷却効率を一層向上させることができるという効果が得られる。   Therefore, the flow rate of a specific flow path part in the cooling medium flow path 54, for example, the cooling medium flow path part 54a can be set higher than the flow rates of the other cooling medium flow path parts 54b to 54d. It becomes possible to effectively cool the vicinity of the remarkable oxidizing gas supply communication hole 30a and the fuel gas supply communication hole 32a. Thereby, the flow rate control of the cooling medium in the separator surface can be easily and reliably performed, the temperature distribution in the separator surface can be controlled well, and the cooling efficiency can be further improved. .

なお、本実施形態では、発電セル12が電解質膜・電極構造体22と第1及び第2セパレータ24、26とを備え、各発電セル12同士が積層されることにより、前記電解質膜・電極構造体22間には、2枚のセパレータである第1及び第2で24、26が介装されている。すなわち、各電解質膜・電極構造体22間には、冷却媒体流路54が形成されている。   In the present embodiment, the power generation cell 12 includes the electrolyte membrane / electrode structure 22 and the first and second separators 24 and 26, and the power generation cells 12 are stacked to form the electrolyte membrane / electrode structure. Between the body 22, 24 and 26 which are the 1st and 2nd which are two separators are interposed. That is, a cooling medium flow path 54 is formed between each electrolyte membrane / electrode structure 22.

これに代えて、例えば、電解質膜・電極構造体22の一方に2枚のセパレータを積層するとともに、前記電解質膜・電極構造体22の他方に1枚のセパレータを積層してもよい。すなわち、電解質膜・電極構造体22間には、1つ置きに冷却媒体流路54が形成される、いわゆる、間引き冷却構造を採用してもよい。   Instead of this, for example, two separators may be stacked on one side of the electrolyte membrane / electrode structure 22, and one separator may be stacked on the other side of the electrolyte membrane / electrode structure 22. That is, a so-called thinning cooling structure in which every other cooling medium flow path 54 is formed between the electrolyte membrane / electrode structures 22 may be employed.

また、第1及び第2凸状部44、48は、ジグザグに構成されているが、これに代えて、湾曲に構成してもよい。   Moreover, although the 1st and 2nd convex-shaped parts 44 and 48 are comprised by the zigzag, it may replace with this and may comprise a curve.

本発明の実施形態に係る燃料電池の概略斜視説明図である。1 is a schematic perspective view of a fuel cell according to an embodiment of the present invention. 前記燃料電池を構成する発電セルの要部分解斜視図である。It is a principal part disassembled perspective view of the electric power generation cell which comprises the said fuel cell. 前記発電セルを構成する第1セパレータの正面図である。It is a front view of the 1st separator which comprises the said electric power generation cell. 前記発電セルを構成する第1及び第2凸状部の斜視説明図である。It is a perspective explanatory view of the 1st and 2nd convex part which constitutes the power generation cell. 前記発電セルを構成する第2セパレータの正面図である。It is a front view of the 2nd separator which constitutes the power generation cell.

符号の説明Explanation of symbols

10…燃料電池 12…発電セル
14…積層体 22…電解質膜・電極構造体
24、26…セパレータ 30a…酸化剤ガス供給連通孔
30b…酸化剤ガス排出連通孔 32a…燃料ガス供給連通孔
32b…燃料ガス排出連通孔 34a…冷却媒体供給連通孔
34b…冷却媒体排出連通孔 36…固体高分子電解質膜
38…アノード側電極 40…カソード側電極
42…燃料ガス流路 42a…燃料ガス流路溝
44、48…凸状部 44a、48a…頂面
46…酸化剤ガス流路 46a…酸化剤ガス流路溝
50…離間部 52…連続接触部
54…冷却媒体流路
DESCRIPTION OF SYMBOLS 10 ... Fuel cell 12 ... Power generation cell 14 ... Laminated body 22 ... Electrolyte membrane electrode assembly 24, 26 ... Separator 30a ... Oxidant gas supply communication hole 30b ... Oxidant gas discharge communication hole 32a ... Fuel gas supply communication hole 32b ... Fuel gas discharge communication hole 34a ... Cooling medium supply communication hole 34b ... Cooling medium discharge communication hole 36 ... Solid polymer electrolyte membrane 38 ... Anode side electrode 40 ... Cathode side electrode 42 ... Fuel gas flow path 42a ... Fuel gas flow path groove 44 48 ... convex portions 44a, 48a ... top surface 46 ... oxidant gas flow path 46a ... oxidant gas flow path groove 50 ... separation part 52 ... continuous contact part 54 ... cooling medium flow path

Claims (2)

電解質の両側にアノード側電極及びカソード側電極が設けられた電解質・電極構造体と、1又は2以上のセパレータとが交互に積層される燃料電池であって、
前記2以上のセパレータは、積層方向に互いに重なり合う第1及び第2セパレータを有し、
前記第1セパレータは、前記アノード側電極に供給される燃料ガスを流通させる複数の燃料ガス流路用第1凹部を設けるとともに、前記第1凹部の裏面側には、長尺な屈曲乃至湾曲する第1凸状部が形成され、
前記第2セパレータは、前記カソード側電極に供給される酸化剤ガスを流通させる複数の酸化剤ガス流路用第2凹部を設けるとともに、前記第2凹部の裏面側には、前記第1凸状部に対向し且つ該第1凸状部と同一方向に延在する長尺な屈曲乃至湾曲する第2凸状部が形成され、
前記第1凸状部の第1頂面と前記第2凸状部の第2頂面とは、互いに離間してセパレータ面方向に冷却媒体を流通させる冷却媒体流路を設けるための離間部と、
所定の長さにわたって互いに積層方向に接触し、前記冷却媒体流路の流れ方向に沿う前記冷却媒体の流通を阻止する封止領域を形成するための連続接触部と、
を構成することを特徴とする燃料電池。
A fuel cell in which an electrolyte / electrode structure in which an anode side electrode and a cathode side electrode are provided on both sides of an electrolyte, and one or more separators are alternately stacked,
The two or more separators have first and second separators that overlap each other in the stacking direction,
The first separator is provided with a plurality of first recesses for a fuel gas flow path through which the fuel gas supplied to the anode-side electrode is circulated, and a long bend or curve is formed on the back side of the first recess. A first convex portion is formed;
The second separator is provided with a plurality of second oxidant gas channel recesses for circulating an oxidant gas supplied to the cathode side electrode, and on the back side of the second recess, the first convex shape A second convex portion that is long and bends or curves opposite to the portion and extends in the same direction as the first convex portion,
The first top surface of the first convex portion and the second top surface of the second convex portion are spaced apart from each other and provided with a cooling medium flow path for circulating the cooling medium in the separator surface direction. ,
A continuous contact portion for forming a sealing region that is in contact with each other over a predetermined length in the stacking direction and prevents the flow of the cooling medium along the flow direction of the cooling medium flow path;
A fuel cell comprising:
請求項1記載の燃料電池において、前記第1及び第2凸状部は、連続して異なる方向に交互に屈曲する第1及び第2屈曲部を有し、
前記離間部では、前記第1及び第2屈曲部の振幅と長さとが同一且つ位相が相違するとともに、
前記連続接触部では、前記第1及び第2屈曲部の位相が一致することを特徴とする燃料電池。
2. The fuel cell according to claim 1, wherein the first and second convex portions have first and second bent portions that are alternately bent in different directions in succession,
In the separation portion, the amplitude and length of the first and second bent portions are the same and have different phases,
In the continuous contact portion, the phase of the first bent portion and the second bent portion coincide with each other.
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KR102055951B1 (en) 2012-12-28 2020-01-23 주식회사 미코 Stack structure for fuel cell
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