JPH08138700A - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPH08138700A JPH08138700A JP6295927A JP29592794A JPH08138700A JP H08138700 A JPH08138700 A JP H08138700A JP 6295927 A JP6295927 A JP 6295927A JP 29592794 A JP29592794 A JP 29592794A JP H08138700 A JPH08138700 A JP H08138700A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst electrode
- fuel cell
- current collecting
- battery cell
- passage
- 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.)
- Granted
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Fuel Cell (AREA)
Abstract
(57)【要約】
【目的】構成部材や電力を取り出す集電部の抵抗過電圧
による電圧低下を軽減する燃料電池を提供する。
【構成】イオン交換膜7の一方面に正の触媒電極8を有
すると共に、他方面に負の触媒電極9を有する電池セル
6を備え、この電池セル6により反応ガスを反応させて
電気を発生させる燃料電池1において、電池セル6はセ
パレータ4で保持され、このセパレータ4に触媒電極と
電通する集電プレート80を配置すると共に、触媒電極
と接触する集電層82,83を設け、この集電層82,
83と集電プレート80とを導電性部材84,85で連
結している。
(57) [Abstract] [Purpose] To provide a fuel cell that alleviates a voltage drop due to a resistance overvoltage of a constituent member and a current collector for extracting electric power. A battery cell 6 having a positive catalyst electrode 8 on one surface of an ion exchange membrane 7 and a negative catalyst electrode 9 on the other surface thereof is provided, and a reaction gas is reacted by the battery cell 6 to generate electricity. In the fuel cell 1 to be operated, the battery cells 6 are held by the separator 4, and the separator 4 is provided with a current collecting plate 80 in electrical communication with the catalyst electrode and provided with current collecting layers 82, 83 in contact with the catalyst electrode. Electric layer 82,
83 and the collector plate 80 are connected by conductive members 84 and 85.
Description
【0001】[0001]
【産業上の利用分野】この発明は、反応ガスを反応させ
て水を生成し、その際に電気を発生させる燃料電池に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel cell in which a reaction gas is reacted to produce water and electricity is generated at that time.
【0002】[0002]
【従来の技術】電気自動車には、例えば燃料電池を搭載
し、この燃料電池によって発生する電気を駆動源として
走行するものがある。この燃料電池は、イオン交換膜の
一方面に正の触媒電極を有すると共に、他方面に負の触
媒電極を有する電池セルを備え、この電池セルにより反
応ガスの水素と酸素とを反応させて水を生成し、その際
に電気を発生させる。2. Description of the Related Art Some electric vehicles are equipped with, for example, a fuel cell and run using electricity generated by the fuel cell as a drive source. This fuel cell is provided with a battery cell having a positive catalyst electrode on one side of the ion exchange membrane and a negative catalyst electrode on the other side of the ion exchange membrane. To generate electricity.
【0003】[0003]
【発明が解決しようとする課題】このように燃料電池の
性能は、図7に示すような電流電圧特性で示され、電圧
理論値より実際の電圧が低下する。この電圧低下の原因
として、例えば燃料電池の触媒電極やその周辺の部材の
構造による活性化過電圧、燃料電池の構成部材や電力を
取り出す集電部の抵抗過電圧、反応ガスの水素、酸素の
供給や反応により生成する水の影響、反応ガス等による
濃度過電圧等が考えられる。As described above, the performance of the fuel cell is shown by the current-voltage characteristic as shown in FIG. 7, and the actual voltage is lower than the theoretical voltage value. The causes of this voltage drop include, for example, activation overvoltage due to the structure of the catalyst electrode of the fuel cell and its surrounding members, resistance overvoltage of the fuel cell constituent members and the current collecting part for extracting electric power, supply of hydrogen and oxygen of the reaction gas, The influence of water generated by the reaction, concentration overvoltage due to reaction gas, etc. are considered.
【0004】特に、この燃料電池の構成部材や電力を取
り出す集電部の抵抗過電圧が生じる具体的な現象とし
て、次のようなものがある。例えば、電池セルにより反
応ガスの水素と酸素とを反応させて水を生成し、その際
に電気を発生させるが、電池セルを積層して電池セルス
タックを構成するようなものでは、リード線等を用いる
と、触媒電極との接続が困難で、また配線のスペースの
確保も容易でないし、しかも電力の取出位置が限定され
る。また、触媒電極との接触抵抗が大きく、効率的な電
力の取出ができない等の問題がある。[0004] In particular, the following are specific phenomena that cause resistance overvoltage in the constituent members of the fuel cell and the current collecting portion for extracting electric power. For example, a battery cell reacts hydrogen and oxygen of a reaction gas to generate water, and electricity is generated at that time. In the case where battery cells are stacked to form a battery cell stack, lead wires, etc. If it is used, it is difficult to connect it to the catalyst electrode, it is not easy to secure a space for wiring, and the power extraction position is limited. Further, there is a problem that the contact resistance with the catalyst electrode is large and the electric power cannot be efficiently extracted.
【0005】この発明は、かかる点に鑑みなされたもの
で、請求項1乃至請求項3記載の発明は、構成部材や電
力を取り出す集電部の抵抗過電圧による電圧低下を軽減
する燃料電池を提供することを目的としている。特に、
請求項1記載の発明は、電池セルから効率的に集電して
電力を取り出すことができ、しかも電力を取出す自由度
が増す燃料電池を提供することを目的としている。ま
た、請求項2記載の発明は、触媒電極との接触抵抗を低
減して、効率的な電力の取出が可能な燃料電池を提供す
ることを目的としている。また、請求項3記載の発明
は、固有抵抗のより低い部材を併用することで集電部の
抵抗を低減すると共に、電力取出しの自由度が増す燃料
電池を提供することを目的としている。The present invention has been made in view of the above points, and the inventions according to claims 1 to 3 provide a fuel cell for reducing a voltage drop due to a resistance overvoltage of a constituent member and a current collecting portion for extracting electric power. The purpose is to do. In particular,
It is an object of the present invention to provide a fuel cell capable of efficiently collecting electric power from a battery cell and taking out electric power, and further increasing the degree of freedom of taking out electric power. It is another object of the present invention to provide a fuel cell capable of efficiently extracting electric power by reducing the contact resistance with the catalyst electrode. It is another object of the present invention to provide a fuel cell in which the resistance of the current collector is reduced by using a member having a lower specific resistance in combination, and the degree of freedom in extracting the power is increased.
【0006】[0006]
【課題を解決するための手段】前記課題を解決するため
に、請求項1記載の発明は、イオン交換膜の一方面に正
の触媒電極を有すると共に、他方面に負の触媒電極を有
する電池セルを備え、この電池セルにより反応ガスを反
応させて電気を発生させる燃料電池において、前記電池
セルはセパレータで保持され、このセパレータに前記触
媒電極と電通する集電プレートを配置すると共に、前記
触媒電極と接触する集電層を設け、この集電層と前記集
電プレートとを導電性部材で連結したことを特徴として
いる。In order to solve the above problems, the invention according to claim 1 has a positive catalyst electrode on one surface of an ion exchange membrane and a negative catalyst electrode on the other surface thereof. In a fuel cell including a cell, in which a reaction gas is reacted by the battery cell to generate electricity, the battery cell is held by a separator, and the separator is provided with a collector plate in electrical communication with the catalyst electrode, and the catalyst The present invention is characterized in that a current collecting layer is provided in contact with the electrodes, and the current collecting layer and the current collecting plate are connected by a conductive member.
【0007】請求項2記載の発明は、前記集電層の表面
に、導電性の軟質材を積層し、この軟質材を前記触媒電
極に接触させたことを特徴としている。According to a second aspect of the present invention, a conductive soft material is laminated on the surface of the current collecting layer, and the soft material is brought into contact with the catalyst electrode.
【0008】請求項3記載の発明は、前記触媒電極の表
面に、カーボン材と導電性の部材との複合層を積層した
ことを特徴としている。The invention according to claim 3 is characterized in that a composite layer of a carbon material and a conductive member is laminated on the surface of the catalyst electrode.
【0009】[0009]
【作用】請求項1記載の発明では、セパレータに触媒電
極と電通する集電プレートを配置すると共に、触媒電極
と接触する集電層を設け、この集電層と集電プレートと
を導電性部材で連結している。このように、集電プレー
トと集電層とを用いることで、例えばリード線等を用い
るものに比して、触媒電極との接続が容易で、また配線
スペースの確保も容易で、しかも集電部の形状やパター
ンを自由に製作できる。従って、電池セルから効率的に
集電して電力を取り出すことができ、しかも集電プレー
トの端部から電力を取出すことができ、燃料電池の組立
の自由度が増す。According to the first aspect of the present invention, the separator is provided with a collector plate in electrical communication with the catalyst electrode, and a collector layer is provided in contact with the catalyst electrode. The collector layer and the collector plate are electrically conductive. Are connected with. As described above, by using the current collecting plate and the current collecting layer, the connection with the catalyst electrode is easier and the wiring space can be secured more easily than the case where the lead wire or the like is used. The shape and pattern of the part can be freely manufactured. Therefore, the power can be efficiently collected from the battery cells to take out the electric power, and the electric power can be taken out from the end portion of the current collecting plate, so that the degree of freedom in assembling the fuel cell is increased.
【0010】請求項2記載の発明では、触媒電極から電
力を取り出す集電部に導電性の軟質材を有するから、面
圧が低くても触媒電極との接触が確実であり、触媒電極
との接触抵抗を低減して、効率的な電力の取出が可能で
ある。According to the second aspect of the present invention, since the current collecting portion for taking out the electric power from the catalyst electrode has the conductive soft material, even if the surface pressure is low, the contact with the catalyst electrode is sure and the contact with the catalyst electrode is ensured. It is possible to reduce contact resistance and extract electric power efficiently.
【0011】請求項3記載の発明では、電池セルの触媒
電極の表面に、カーボン材と導電性の部材との複合層を
積層したから、触媒電極の固有抵抗を低減して、効率的
な電力の取出が可能である。また、触媒電極の任意の位
置から効率的に電力を取出すことができ、電力取出の自
由度が増す。According to the third aspect of the present invention, since the composite layer of the carbon material and the conductive member is laminated on the surface of the catalyst electrode of the battery cell, the specific resistance of the catalyst electrode is reduced and efficient power consumption is achieved. Can be taken out. Further, electric power can be efficiently taken out from any position of the catalyst electrode, and the degree of freedom in taking out electric power is increased.
【0012】[0012]
【実施例】以下、この発明の燃料電池の実施例を図面に
基づいて詳細に説明する。Embodiments of the fuel cell of the present invention will be described below in detail with reference to the drawings.
【0013】図1乃至図3は請求項1記載の燃料電池の
実施例を示し、図1は燃料電池の縦断面図、図2は図1
のII-II線に沿う断面図、図3は燃料電池の電力取出部
の断面図である。この燃料電池1は、組付軸2により組
み付けられた電池セルスタック3を備えている。電池セ
ルスタック3はセパレータ4及び電池セル6ガ交互に複
数積層して組み付けて構成され、セパレータ4はガスケ
ット4a、集電プレート80、ガスケット4bから構成
される。セパレータ4,4の間には、電池セル6が備え
られている。電池セル6の面方向を上下方向に向け、か
つ電池セルスタック3の設置方向L1に対して電池セル
の配置方向L2を角度α傾斜して設けて配置されてい
る。1 to 3 show an embodiment of a fuel cell according to claim 1, FIG. 1 is a longitudinal sectional view of the fuel cell, and FIG. 2 is FIG.
2 is a cross-sectional view taken along line II-II, and FIG. 3 is a cross-sectional view of an electric power extracting portion of the fuel cell. The fuel cell 1 includes a battery cell stack 3 assembled by an assembly shaft 2. The battery cell stack 3 is formed by alternately stacking a plurality of separators 4 and battery cells 6 and assembling them. The separator 4 is composed of a gasket 4a, a current collecting plate 80, and a gasket 4b. A battery cell 6 is provided between the separators 4 and 4. The battery cell 6 is arranged such that the surface direction of the battery cell 6 is oriented in the up-down direction and the arrangement direction L2 of the battery cell is inclined by an angle α with respect to the installation direction L1 of the battery cell stack 3.
【0014】電池セル6は、イオン交換膜7、正の触媒
電極8及び負の触媒電極9から構成されている。イオン
交換膜7の外周部7aは、セパレータ4のガスケット4
bと、対向するセパレータ4のガスケット4aとの間に
挟んで保持され、電池セル6により反応ガスの水素と酸
素とを反応させて電気を発生し、その際に水が生成す
る。The battery cell 6 is composed of an ion exchange membrane 7, a positive catalyst electrode 8 and a negative catalyst electrode 9. The outer peripheral portion 7a of the ion exchange membrane 7 is the gasket 4 of the separator 4.
It is sandwiched and held between b and the gasket 4a of the opposing separator 4, and the battery cells 6 react hydrogen and oxygen of the reaction gas to generate electricity, and water is generated at that time.
【0015】電池セル6の正の触媒電極8の外側には、
ガスケット4bの溝部4c側が正の触媒電極8に接触
し、ガスケット4bの溝4cにより連通する反応ガス通
路12が設けられている。電池セル6の負の触媒電極9
の外側には、ガスケット4aの溝部4d側が負の触媒電
極9に接触し、ガスケット4aの溝4dにより連通する
反応ガス通路13が設けられ、この反応ガス通路13は
反応ガス通路12に対して直交する方向に配置されてい
る。Outside the positive catalyst electrode 8 of the battery cell 6,
A reaction gas passage 12 is provided in which the groove 4c side of the gasket 4b is in contact with the positive catalyst electrode 8 and communicates with the groove 4c of the gasket 4b. Negative catalyst electrode 9 of battery cell 6
A reaction gas passage 13 that contacts the negative catalyst electrode 9 on the groove 4d side of the gasket 4a and communicates with the groove 4d of the gasket 4a is provided outside the reaction gas passage 13. The reaction gas passage 13 is orthogonal to the reaction gas passage 12. It is arranged in the direction to.
【0016】電池セル6の周囲を囲むセパレータ4,4
のガスケット4b,4aとイオン交換膜7の端部7aと
の間にOリング14a,14bが設けられ、Oリング1
4a,14bにより電池セル6をシールしている。電池
セルスタック3の左側上方の隅部には水素の入口部15
が設けられ、右側下方の隅部には水素の出口部16が設
けられ、入口部15及び出口部16の周囲を囲むように
ガスケット4bとガスケット5aとの間にOリング1
7,18が設けられ、入口部15及び出口部16をシー
ルしている。入口部15には、電池セル6の積層方向に
反応ガス通路の入口通路15aが形成され、この入口通
路15aから4個のトンネル通路15bがOリング14
a,14bの下方を通って電池セル6の分配通路15c
に連通し、分配通路15cから反応ガス通路13に連通
している。出口部16には、電池セル6の積層方向に反
応ガス通路の出口通路16aが形成され、この出口通路
16aに連通された4個のトンネル通路16bはOリン
グ14a,14bの下方を通って電池セル6の集合通路
16cに連通し、集合通路16cは反応ガス通路13と
連通している。Separator 4, 4 surrounding the battery cell 6
The O-rings 14a and 14b are provided between the gaskets 4b and 4a of FIG.
The battery cell 6 is sealed by 4a and 14b. At the upper left corner of the battery cell stack 3, a hydrogen inlet 15 is provided.
And a hydrogen outlet 16 is provided in the lower right corner, and an O-ring 1 is provided between the gasket 4b and the gasket 5a so as to surround the inlet 15 and the outlet 16.
7 and 18 are provided to seal the inlet portion 15 and the outlet portion 16. An inlet passage 15a of the reaction gas passage is formed in the inlet portion 15 in the stacking direction of the battery cells 6, and four tunnel passages 15b are formed from the inlet passage 15a to the O-ring 14.
distribution passage 15c of the battery cell 6 passing below a and 14b
And from the distribution passage 15c to the reaction gas passage 13. An outlet passage 16a of a reaction gas passage is formed in the outlet portion 16 in the stacking direction of the battery cells 6, and the four tunnel passages 16b communicating with the outlet passage 16a pass under the O-rings 14a and 14b. It communicates with the collecting passage 16c of the cell 6, and the collecting passage 16c communicates with the reaction gas passage 13.
【0017】電池セルスタック3の上方右側の隅部には
酸素の入口部19が設けられ、下方左側の隅部には酸素
の出口部20が設けられ、入口部19及び出口部20の
周囲を囲むようにガスケット4bとガスケット4aの間
にOリング21,22が設けられ、入口部19及び出口
部20をシールしている。入口部19には、電池セル6
の積層方向に反応ガス通路の入口通路19aが形成さ
れ、この入口通路19aから4個のトンネル通路19b
がOリング14a,14bの下方を通って電池セル6の
分配通路19cに連通し、分配通路19cから反応ガス
通路12に連通している。出口部20には、電池セル6
の積層方向に反応ガス通路の出口通路20aが形成さ
れ、この出口通路20aに連通された4個のトンネル通
路20bはOリング14の下方を通って電池セル6の集
合通路20cに連通し、集合通路20cは反応ガス通路
12と連通している。An oxygen inlet portion 19 is provided at the upper right corner of the battery cell stack 3, and an oxygen outlet portion 20 is provided at the lower left corner thereof. O-rings 21 and 22 are provided between the gasket 4b and the gasket 4a so as to surround them, and seal the inlet portion 19 and the outlet portion 20. At the inlet portion 19, the battery cell 6
An inlet passage 19a of the reaction gas passage is formed in a stacking direction of the four tunnel passages 19b from the inlet passage 19a.
Communicates with the distribution passage 19c of the battery cell 6 passing below the O-rings 14a and 14b, and from the distribution passage 19c to the reaction gas passage 12. At the outlet portion 20, the battery cell 6
The outlet passage 20a of the reaction gas passage is formed in the stacking direction of the four, and the four tunnel passages 20b communicating with the outlet passage 20a communicate with the collecting passage 20c of the battery cell 6 passing under the O-ring 14. The passage 20c communicates with the reaction gas passage 12.
【0018】また、セパレータ4bには水通路23が形
成されている。水通路23の一方23aはトンネル通路
24aを介して水素の入口部15の近傍で上側に設けら
れた排出部24に連通され、他方23bはトンネル通路
25aを介して水素の出口部16の近傍で下側に設けら
れた供給部25に連通されている。排出部24及び供給
部25の周囲を囲むようにガスケット4bとガスケット
4aの間にOリング26a,27aが設けられ、排出部
24及び供給部25をシールしている。A water passage 23 is formed in the separator 4b. One side 23a of the water passage 23 is connected to the discharge part 24 provided on the upper side in the vicinity of the hydrogen inlet part 15 via the tunnel passage 24a, and the other side 23b is near the hydrogen outlet part 16 via the tunnel passage 25a. It communicates with the supply unit 25 provided on the lower side. O-rings 26a and 27a are provided between the gasket 4b and the gasket 4a so as to surround the discharge portion 24 and the supply portion 25, and seal the discharge portion 24 and the supply portion 25.
【0019】また、セパレータ4aには水通路28が形
成されている。水通路28の一方28aはトンネル通路
29aを介して酸素の入口部19の近傍で右側に設けら
れた排出部29に連通され、他方28bはトンネル通路
30aを介して酸素の出口部20の近傍で左側に設けら
れた供給部30に連通されている。排出部29及び供給
部30の周囲を囲むようにガスケット4bとガスケット
4aの間にOリング26b,27bが設けられ、排出部
29及び供給部30をシールしている。A water passage 28 is formed in the separator 4a. One of the water passages 28a communicates with a discharge portion 29 provided on the right side near the oxygen inlet portion 19 through a tunnel passage 29a, and the other 28b near the oxygen outlet portion 20 through a tunnel passage 30a. It communicates with the supply unit 30 provided on the left side. O-rings 26b and 27b are provided between the gasket 4b and the gasket 4a so as to surround the discharge unit 29 and the supply unit 30, and seal the discharge unit 29 and the supply unit 30.
【0020】電池セルスタック3の水素の入口部15か
ら加温、加湿した水素を供給すると、この水分を含む水
素は入口通路15aからセパレータ4aのトンネル通路
15bを通って分配通路15cに導かれ、分配通路15
cから反応ガス通路13を流れる。一方、酸素の入口部
19から加温、加湿した酸素を供給すると、この水分を
含む酸素は入口通路19aからセパレータ4bのトンネ
ル通路19bを通って分配通路19cに連通し、分配通
路19cから反応ガス通路12を流れる。When heated and humidified hydrogen is supplied from the hydrogen inlet 15 of the battery cell stack 3, the hydrogen containing water is introduced from the inlet passage 15a to the distribution passage 15c through the tunnel passage 15b of the separator 4a. Distribution passage 15
The reaction gas passage 13 flows from c. On the other hand, when heated and humidified oxygen is supplied from the oxygen inlet portion 19, the oxygen containing water communicates with the distribution passage 19c from the inlet passage 19a through the tunnel passage 19b of the separator 4b and the reaction gas from the distribution passage 19c. Flow through passage 12.
【0021】このとき、電池セル6により反応ガスの水
素と酸素の電気化学的な反応により水を生成し、その際
の自由エネルギーの変化を電気エネルギーとして取り出
す発電が行われる。また、主として水素と水は電池セル
6の集合通路16cに集められ、トンネル通路16bを
通って出口通路16aに導かれて出口部16から排出さ
れる。主として酸素と水は電池セル6の集合通路20c
に集められ、トンネル通路20bを通って出口通路20
aに導かれて出口部20から排出される。At this time, power is generated by the battery cell 6 to generate water by an electrochemical reaction of hydrogen and oxygen of the reaction gas, and to extract the change in free energy at that time as electric energy. Further, mainly hydrogen and water are collected in the collecting passage 16c of the battery cell 6, are guided to the outlet passage 16a through the tunnel passage 16b, and are discharged from the outlet portion 16. Mainly oxygen and water are the collecting passages 20c for the battery cells 6.
Collected at the exit passage 20 through the tunnel passage 20b.
It is guided to a and discharged from the outlet portion 20.
【0022】電池セル6による水素と酸素の電気化学的
な反応は、一方では酸素と水が正の触媒電極8を通り、
イオン交換膜7の表面に供給され、他方では水素と水が
負の触媒電極9を通り、イオン交換膜7の表面に供給さ
れ、この正の触媒電極8とイオン交換膜7の界面及び負
の触媒電極9とイオン交換膜7の界面で行われる。On the other hand, the electrochemical reaction of hydrogen and oxygen by the battery cell 6 is such that oxygen and water pass through the positive catalytic electrode 8,
On the other hand, hydrogen and water are supplied to the surface of the ion exchange membrane 7, pass through the negative catalyst electrode 9 and are supplied to the surface of the ion exchange membrane 7, and the interface between the positive catalyst electrode 8 and the ion exchange membrane 7 and the negative It is performed at the interface between the catalyst electrode 9 and the ion exchange membrane 7.
【0023】セパレータ4のガスケット4a,4bの間
には、集電プレート80が設けられ、さらにガスケット
4a,4bの外側には触媒電極と接触する集電層82,
83を設け、集電層82と集電プレート80とを導電性
部材84で連結し、集電層83と集電プレート80とを
導電性部材85で連結している。A collector plate 80 is provided between the gaskets 4a and 4b of the separator 4, and a collector layer 82, which contacts the catalyst electrode, is provided outside the gaskets 4a and 4b.
83 is provided, the current collecting layer 82 and the current collecting plate 80 are connected by the conductive member 84, and the current collecting layer 83 and the current collecting plate 80 are connected by the conductive member 85.
【0024】集電プレート80は銅箔で形成され、この
集電プレート80の上下面にはそれぞれ水通路28,2
3が形成されている。集電層82は、例えばガスケット
4aの表面に、銅箔82aを設け、さらに銅箔82aに
金メッキ82bを設けて構成されている。また、集電層
83も同様に、例えばガスケット4bの表面に、銅箔8
3aを設け、さらに銅箔83aに金メッキ83bを設け
て構成されている。The current collecting plate 80 is made of copper foil, and water channels 28 and 2 are formed on the upper and lower surfaces of the current collecting plate 80, respectively.
3 are formed. The current collecting layer 82 is configured, for example, by providing a copper foil 82a on the surface of the gasket 4a and further providing a gold plating 82b on the copper foil 82a. Similarly, for the current collecting layer 83, for example, the copper foil 8
3a is provided, and further gold plating 83b is provided on the copper foil 83a.
【0025】導電性部材84は、例えばガスケット4a
に形成した孔4a1に銅メッキ84aを設け、さらに銅
メッキ84a上に金メッキ84bを設けて構成され、こ
の導電性部材84により触媒電極側と水通路28とを連
通する水通路28fが形成される。また、同様に、導電
性部材85は、例えばガスケット4bに形成した孔4b
1に銅メッキ85aを設け、さらに銅メッキ85a上に
金メッキ85bを設けて構成され、この導電性部材85
により触媒電極側と水通路23とを連通する水通路23
fが形成される。The conductive member 84 is, for example, the gasket 4a.
The hole 4a1 formed in 1 is provided with a copper plating 84a, and further a gold plating 84b is provided on the copper plating 84a. The conductive member 84 forms a water passage 28f that connects the catalyst electrode side and the water passage 28. . Similarly, the conductive member 85 has a hole 4b formed in the gasket 4b, for example.
1 is provided with a copper plating 85a, and further a gold plating 85b is provided on the copper plating 85a.
The water passage 23 that connects the catalyst electrode side and the water passage 23 with each other
f is formed.
【0026】このように、セパレータ4に触媒電極と電
通する集電プレート80を配置すると共に、触媒電極と
接触する集電層82,83を設け、この集電層82,8
3と集電プレート80とを導電性部材84,85で連結
している。この集電プレート80の端部に、例えばリー
ド線等を接続して電離セル6の正の触媒電極8及び負の
触媒電極9から電力を取り出す。As described above, the current collecting plate 80 which is in electrical communication with the catalyst electrode is arranged on the separator 4, and the current collecting layers 82 and 83 which are in contact with the catalyst electrode are provided.
3 and the collector plate 80 are connected by conductive members 84 and 85. For example, a lead wire or the like is connected to the end portion of the current collecting plate 80 to take out electric power from the positive catalyst electrode 8 and the negative catalyst electrode 9 of the ionization cell 6.
【0027】この発明では、集電層82,83を用いる
ことで、例えばリード線等を用いるものに比して、触媒
電極との接続が容易で、また配線スペースの確保も容易
で、しかも集電部の形状やパターンを自由に製作でき
る。従って、電池セル6から効率的に集電して電力を取
り出すことができ、しかもプリント基板等の方法を用い
て集電プレート80の端部から電力を取出すことがで
き、燃料電池1の組立の自由度が増す。In the present invention, by using the current collecting layers 82 and 83, the connection with the catalyst electrode is easier and the wiring space can be secured more easily than the one using the lead wire or the like. The shape and pattern of the electric part can be freely manufactured. Therefore, the power can be efficiently collected from the battery cells 6 to take out the electric power, and the electric power can be taken out from the end portion of the current collecting plate 80 by using a method such as a printed circuit board. The degree of freedom increases.
【0028】図4は請求項2記載の集電層の実施例を示
す断面図である。この実施例の正の触媒電極8と接触す
る集電層83は、集電材83cに導電性の軟質材83d
を積層して形成される。導電性の軟質材83dは、例え
ば、導電性の金属箔、金メッキ層等により構成される。
また、負の触媒電極9と接触する集電層82は、集電材
82cに導電性の軟質材82dを積層して形成される。
導電性の軟質材82dは、例えば、導電性の金属箔、金
メッキ層等により構成される。FIG. 4 is a sectional view showing an embodiment of the current collecting layer according to the second aspect. The current collecting layer 83 in contact with the positive catalyst electrode 8 of this embodiment has a conductive soft material 83d as the current collecting material 83c.
Are formed by stacking. The conductive soft material 83d is composed of, for example, a conductive metal foil, a gold plating layer, or the like.
Further, the current collecting layer 82 in contact with the negative catalyst electrode 9 is formed by laminating the conductive soft material 82d on the current collecting material 82c.
The conductive soft material 82d is composed of, for example, a conductive metal foil, a gold plating layer, or the like.
【0029】従って、燃料電池1の組立により締付の面
圧が低くても集電層83,82と触媒電極8,9との接
触が確実であり、触媒電極との接触抵抗を低減して、効
率的な電力の取出が可能である。Therefore, even if the surface pressure of tightening is low due to the assembly of the fuel cell 1, the contact between the current collecting layers 83, 82 and the catalyst electrodes 8, 9 is reliable, and the contact resistance with the catalyst electrodes is reduced. It is possible to take out electric power efficiently.
【0030】図5及び図6は請求項3記載の触媒電極の
実施例を示す図である。この実施例では、正及び負の触
媒電極8,9の表面に、カーボン材と導電性の部材との
複合層85を積層している。図5の実施例では、複合層
85がカーボン材85aに導電性の金属繊維85bを混
入して形成され、図6の実施例では、複合層85がカー
ボン材85cに金メッキ層85dを積層して形成されて
いる。5 and 6 are views showing an embodiment of the catalyst electrode according to the third aspect. In this embodiment, a composite layer 85 of a carbon material and a conductive member is laminated on the surfaces of the positive and negative catalyst electrodes 8 and 9. In the embodiment of FIG. 5, the composite layer 85 is formed by mixing the conductive metal fiber 85b into the carbon material 85a, and in the embodiment of FIG. 6, the composite layer 85 is formed by laminating the gold plating layer 85d on the carbon material 85c. Has been formed.
【0031】このように、電池セル6の正及び負の触媒
電極8,9の表面に、カーボン材と導電性の部材との複
合層85を積層したから、正及び負の触媒電極8,9の
固有抵抗を低減して、効率的な電力の取出が可能であ
る。また、正及び負の触媒電極8,9の任意の位置から
効率的に電力を取出すことができ、電力取出の自由度が
増す。また、正及び負の触媒電極8,9は、基材にカー
ボン材を使用している場合が多いいので触媒電極そのも
のに導電性部材を複合化させたり、表面に金メッキ層を
積層しても良い。As described above, since the composite layer 85 of the carbon material and the conductive member is laminated on the surfaces of the positive and negative catalyst electrodes 8 and 9 of the battery cell 6, the positive and negative catalyst electrodes 8 and 9 are formed. It is possible to efficiently extract the electric power by reducing the specific resistance of. Moreover, electric power can be efficiently taken out from any positions of the positive and negative catalyst electrodes 8 and 9, and the degree of freedom of taking out electric power is increased. In addition, since the positive and negative catalyst electrodes 8 and 9 often use a carbon material as a base material, even if a conductive member is combined with the catalyst electrode itself or a gold plating layer is laminated on the surface. good.
【0032】[0032]
【発明の効果】前記したように、請求項1記載の発明
は、セパレータに触媒電極と電通する集電プレートを配
置すると共に、触媒電極と接触する集電層を設け、この
集電層と集電プレートとを導電性部材で連結したから、
集電プレートと集電層とを用いることで、例えばリード
線等を用いるものに比して、触媒電極との接続が容易
で、また配線スペースの確保も容易で、しかも集電部の
形状やパターンを自由に製作できる。従って、電池セル
から効率的に集電して電力を取り出すことができ、しか
も集電プレートの端部から電力を取出すことができ、燃
料電池の組立の自由度が増す。As described above, according to the first aspect of the present invention, the separator is provided with the current collecting plate that is in electrical communication with the catalyst electrode, and the current collecting layer that is in contact with the catalyst electrode is provided. Since it is connected to the electric plate with a conductive member,
By using the current collecting plate and the current collecting layer, it is easier to connect to the catalyst electrode and to secure a wiring space, and the shape and shape of the current collecting portion are improved as compared with those using a lead wire or the like. You can freely create patterns. Therefore, the power can be efficiently collected from the battery cells to take out the electric power, and the electric power can be taken out from the end portion of the current collecting plate, so that the degree of freedom in assembling the fuel cell is increased.
【0033】請求項2記載の発明は、触媒電極から電力
を取り出す集電部に導電性の軟質材を有するから、面圧
が低くても触媒電極との接触が確実であり、触媒電極と
の接触抵抗を低減して、効率的な電力の取出が可能であ
る。According to the second aspect of the present invention, since the current collecting portion for taking out the electric power from the catalyst electrode has a conductive soft material, even if the surface pressure is low, the contact with the catalyst electrode is sure and the contact with the catalyst electrode is ensured. It is possible to reduce contact resistance and extract electric power efficiently.
【0034】請求項3記載の発明は、電池セルの触媒電
極の表面に、カーボン材と導電性の部材との複合層を積
層したから、触媒電極の固有抵抗を低減して、効率的な
電力の取出が可能である。また、触媒電極の任意の位置
から効率的に電力を取出すことができ、電力取出の自由
度が増す。According to the third aspect of the present invention, since the composite layer of the carbon material and the conductive member is laminated on the surface of the catalyst electrode of the battery cell, the specific resistance of the catalyst electrode is reduced to achieve efficient power consumption. Can be taken out. Further, electric power can be efficiently taken out from any position of the catalyst electrode, and the degree of freedom in taking out electric power is increased.
【図1】請求項1記載の燃料電池の正面図である。FIG. 1 is a front view of a fuel cell according to claim 1.
【図2】図1のII-II線に沿う断面図である。FIG. 2 is a sectional view taken along line II-II in FIG.
【図3】燃料電池の電力取出部の断面図である。FIG. 3 is a cross-sectional view of a power extraction unit of a fuel cell.
【図4】請求項2記載の燃料電池の実施例の概略構成を
示す断面図である。FIG. 4 is a cross-sectional view showing a schematic configuration of an embodiment of the fuel cell according to claim 2.
【図5】請求項3記載の燃料電池の実施例の概略構成を
示す図である。FIG. 5 is a diagram showing a schematic configuration of an embodiment of the fuel cell according to claim 3;
【図6】請求項3記載の燃料電池の他の実施例の概略構
成を示す図である。FIG. 6 is a diagram showing a schematic configuration of another embodiment of the fuel cell according to claim 3;
【図7】燃料電池の電流電圧特性を示す図である。FIG. 7 is a diagram showing current-voltage characteristics of a fuel cell.
1 燃料電池 4 セパレータ 6 電池セル 7 イオン交換膜 8,9 触媒電極 80,90 集電プレート 82,83 集電層 84,85 導電性部材 1 Fuel Cell 4 Separator 6 Battery Cell 7 Ion Exchange Membrane 8, 9 Catalyst Electrode 80, 90 Current Collection Plate 82, 83 Current Collection Layer 84, 85 Conductive Member
Claims (3)
すると共に、他方面に負の触媒電極を有する電池セルを
備え、この電池セルにより反応ガスを反応させて電気を
発生させる燃料電池において、前記電池セルはセパレー
タで保持され、このセパレータに前記触媒電極と電通す
る集電プレートを配置すると共に、前記触媒電極と接触
する集電層を設け、この集電層と前記集電プレートとを
導電性部材で連結したことを特徴とする燃料電池。1. A fuel cell comprising a battery cell having a positive catalyst electrode on one surface of an ion exchange membrane and a negative catalyst electrode on the other surface thereof, the reaction gas being reacted by the battery cell to generate electricity. In the above, the battery cell is held by a separator, and a current collector plate that is in electrical communication with the catalyst electrode is disposed on the separator, and a current collector layer that is in contact with the catalyst electrode is provided, and the current collector layer and the current collector plate are provided. A fuel cell, wherein the fuel cells are connected by a conductive member.
層し、この軟質材を前記触媒電極に接触させたことを特
徴とする請求項1記載の燃料電池。2. The fuel cell according to claim 1, wherein a conductive soft material is laminated on the surface of the current collecting layer, and the soft material is brought into contact with the catalyst electrode.
性の部材との複合層を積層したことを特徴とする請求項
1記載の燃料電池。3. The fuel cell according to claim 1, wherein a composite layer of a carbon material and a conductive member is laminated on the surface of the catalyst electrode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29592794A JP3465830B2 (en) | 1994-11-04 | 1994-11-04 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29592794A JP3465830B2 (en) | 1994-11-04 | 1994-11-04 | Fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH08138700A true JPH08138700A (en) | 1996-05-31 |
| JP3465830B2 JP3465830B2 (en) | 2003-11-10 |
Family
ID=17826930
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29592794A Expired - Fee Related JP3465830B2 (en) | 1994-11-04 | 1994-11-04 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3465830B2 (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999052165A1 (en) * | 1998-04-03 | 1999-10-14 | Plug Power, Inc. | Fuel cell fluid flow plate having conductivity and increased non-conductive material |
| FR2781606A1 (en) * | 1998-07-21 | 2000-01-28 | Sorapec | NEW BIPOLAR COLLECTOR FOR FUEL CELL |
| WO2000002270A3 (en) * | 1998-07-01 | 2000-04-13 | British Gas Plc | A printed circuit board separator for an electrochemical fuel cell |
| WO2000060686A1 (en) * | 1999-04-07 | 2000-10-12 | Sorapec | Bipolar collector characterised by discrete collecting of charges |
| WO2001024295A1 (en) * | 1999-09-30 | 2001-04-05 | Sorapec | Bipolar collectors for pem-effect fuel cells |
| EP1152477A2 (en) | 2000-05-02 | 2001-11-07 | Honda Giken Kogyo Kabushiki Kaisha | Polymeric membrane fuel cell |
| JP2001319667A (en) * | 2000-05-02 | 2001-11-16 | Honda Motor Co Ltd | Fuel cell |
| JP2001319666A (en) * | 2000-05-02 | 2001-11-16 | Honda Motor Co Ltd | Fuel cell and method of manufacturing the same |
| JP2005531911A (en) * | 2002-07-02 | 2005-10-20 | マイクロセル コーポレーション | Microcell electrochemical apparatus and assembly with corrosion-resistant current collector and method of manufacturing the same |
| JP2008021549A (en) * | 2006-07-13 | 2008-01-31 | Casio Comput Co Ltd | Separator, fuel cell device and electronic device |
| US7695843B2 (en) | 2004-02-13 | 2010-04-13 | Microcell Corporation | Microfibrous fuel cell assemblies comprising fiber-supported electrocatalyst layers, and methods of making same |
| US8048584B2 (en) | 2003-03-07 | 2011-11-01 | Microcell Corporation | Fuel cell structures and assemblies |
| US8168350B1 (en) | 2002-07-02 | 2012-05-01 | Microcell Corporation | Fuel cell structures and assemblies with channeled current collectors, and method of making the same |
-
1994
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Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999052165A1 (en) * | 1998-04-03 | 1999-10-14 | Plug Power, Inc. | Fuel cell fluid flow plate having conductivity and increased non-conductive material |
| US6541147B1 (en) | 1998-07-01 | 2003-04-01 | Ballard Power Systems Inc. | Printed circuit board separator for an electrochemical fuel cell |
| WO2000002270A3 (en) * | 1998-07-01 | 2000-04-13 | British Gas Plc | A printed circuit board separator for an electrochemical fuel cell |
| FR2781606A1 (en) * | 1998-07-21 | 2000-01-28 | Sorapec | NEW BIPOLAR COLLECTOR FOR FUEL CELL |
| WO2000005775A1 (en) * | 1998-07-21 | 2000-02-03 | Sorapec | Bipolar collector for fuel cell |
| WO2000060686A1 (en) * | 1999-04-07 | 2000-10-12 | Sorapec | Bipolar collector characterised by discrete collecting of charges |
| FR2792114A1 (en) * | 1999-04-07 | 2000-10-13 | Sorapec | IMPROVEMENT FOR BIPOLAR COLLECTORS CHARACTERIZED BY A DISCRETE COLLECTION OF LOADS |
| WO2001024295A1 (en) * | 1999-09-30 | 2001-04-05 | Sorapec | Bipolar collectors for pem-effect fuel cells |
| FR2799308A1 (en) * | 1999-09-30 | 2001-04-06 | Sorapec | IMPROVEMENTS ON BIPOLAR COLLECTORS FOR PEM-TYPE FUEL CELLS |
| EP1152477A2 (en) | 2000-05-02 | 2001-11-07 | Honda Giken Kogyo Kabushiki Kaisha | Polymeric membrane fuel cell |
| JP2001319666A (en) * | 2000-05-02 | 2001-11-16 | Honda Motor Co Ltd | Fuel cell and method of manufacturing the same |
| JP2001319667A (en) * | 2000-05-02 | 2001-11-16 | Honda Motor Co Ltd | Fuel cell |
| EP1152477A3 (en) * | 2000-05-02 | 2007-03-14 | Honda Giken Kogyo Kabushiki Kaisha | Polymeric membrane fuel cell |
| JP2005531911A (en) * | 2002-07-02 | 2005-10-20 | マイクロセル コーポレーション | Microcell electrochemical apparatus and assembly with corrosion-resistant current collector and method of manufacturing the same |
| JP4783570B2 (en) * | 2002-07-02 | 2011-09-28 | マイクロセル コーポレーション | Microcell electrochemical apparatus and assembly with corrosion-resistant current collector and method of manufacturing the same |
| US8168350B1 (en) | 2002-07-02 | 2012-05-01 | Microcell Corporation | Fuel cell structures and assemblies with channeled current collectors, and method of making the same |
| US8048584B2 (en) | 2003-03-07 | 2011-11-01 | Microcell Corporation | Fuel cell structures and assemblies |
| US7695843B2 (en) | 2004-02-13 | 2010-04-13 | Microcell Corporation | Microfibrous fuel cell assemblies comprising fiber-supported electrocatalyst layers, and methods of making same |
| JP2008021549A (en) * | 2006-07-13 | 2008-01-31 | Casio Comput Co Ltd | Separator, fuel cell device and electronic device |
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| Publication number | Publication date |
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| JP3465830B2 (en) | 2003-11-10 |
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