JPH0594832A - Solid high molecular electrolyte type fuel cell - Google Patents
Solid high molecular electrolyte type fuel cellInfo
- Publication number
- JPH0594832A JPH0594832A JP3252637A JP25263791A JPH0594832A JP H0594832 A JPH0594832 A JP H0594832A JP 3252637 A JP3252637 A JP 3252637A JP 25263791 A JP25263791 A JP 25263791A JP H0594832 A JPH0594832 A JP H0594832A
- Authority
- JP
- Japan
- Prior art keywords
- reaction gas
- cell
- humidifier
- polymer electrolyte
- fuel cell
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04119—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0065—Solid electrolytes
- H01M2300/0082—Organic polymers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04097—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the reactants
-
- 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
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は固体高分子電解質型燃
料電池に係り、特に固体高分子電解質の含水量を最適状
態に保持する固体高分子電解質型燃料電池に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid polymer electrolyte fuel cell, and more particularly to a solid polymer electrolyte fuel cell which maintains an optimum water content of the solid polymer electrolyte.
【0002】[0002]
【従来の技術】固体高分子電解質型燃料電池は固体高分
子電解質膜の二つの主面にそれぞれアノードまたはカソ
ードおよび電極基材を配して形成される。アノードまた
はカソードの各電極は固体高分子電解質膜と電極基材と
により挟まれる。固体高分子電解質膜はスルホン酸基を
持つポリスチレン系の陽イオン交換膜をカチオン導電性
膜として使用したもの、フロロカーボンスルホン酸とポ
リビニリデンフロライドの混合膜、あるいはフロロカー
ボンマトリックスにトリフロロエチレンをグラフト化し
たものなどが知られているが最近ではパーフロロカーボ
ンスルホン酸膜を用いて燃料電池の長寿命化を図ったも
のが知られるに至った。2. Description of the Related Art A solid polymer electrolyte fuel cell is formed by disposing an anode or a cathode and an electrode base material on each of two main surfaces of a solid polymer electrolyte membrane. Each anode or cathode electrode is sandwiched between the solid polymer electrolyte membrane and the electrode base material. The solid polymer electrolyte membrane uses a polystyrene cation exchange membrane with sulfonic acid groups as the cation conductive membrane, a mixed membrane of fluorocarbon sulfonic acid and polyvinylidene fluoride, or trifluoroethylene grafted to the fluorocarbon matrix. However, recently, a perfluorocarbon sulfonic acid membrane has been used to extend the life of a fuel cell.
【0003】固体高分子電解質膜は分子中にプロトン
(水素イオン)交換基を有し、飽和に含水させることに
より常温で20Ω・cm以下の比抵抗を示しプロトン導
電性電解質として機能する。飽和含水量は温度によって
可逆的に変化する。電極基材は多孔質体で燃料電池の反
応ガス供給手段または反応ガス排出手段および集電体と
して機能する。アノードまたはカソードの電極において
は三相界面が形成され電気化学反応が起こる。The solid polymer electrolyte membrane has a proton (hydrogen ion) exchange group in the molecule, and when it is saturated to contain water, it exhibits a specific resistance of 20 Ω · cm or less at room temperature and functions as a proton conductive electrolyte. The saturated water content changes reversibly with temperature. The electrode base material is a porous body and functions as a reaction gas supply means or a reaction gas discharge means of the fuel cell and a current collector. At the anode or cathode electrode, a three-phase interface is formed and an electrochemical reaction occurs.
【0004】アノードでは(1)式の反応が起きる。 H2 =2H+ +2e (1) カソードでは(2)式の反応が起こる。 1/2O2 +2H+ +2e=H2 O (2)At the anode, the reaction of the formula (1) occurs. H 2 = 2H + + 2e (1) At the cathode, the reaction of the formula (2) occurs. 1 / 2O 2 + 2H + + 2e = H 2 O (2)
【0005】つまりアノードにおいては系の外部より供
給された水素がプロトンと電子を生成する。生成したプ
ロトンはイオン交換膜中をカソードにむかって移動し電
子は外部回路を通ってカソードに移動する。一方カソー
ドにおいては系の外部より供給された酸素とイオン交換
膜中をアノードより移動してきたプロトンと外部回路よ
り移動してきた電子が反応し、水を生成する。That is, at the anode, hydrogen supplied from outside the system produces protons and electrons. The generated protons move toward the cathode in the ion exchange membrane, and the electrons move to the cathode through an external circuit. On the other hand, in the cathode, oxygen supplied from the outside of the system reacts with protons moving from the anode in the ion exchange membrane and electrons moving from the external circuit to generate water.
【0006】このような固体高分子電解質型燃料電池に
おいてはプロトンがアノードよりカソードに向かってイ
オン交換膜中を移動する際に水和の状態で移動するため
アノード近傍では含水量が減少しイオン交換膜が乾いて
くる。そのためにアノード近傍では水を供給しないとプ
ロトンの移動が困難になる。また酸化剤として空気を用
いる場合は理論消費量の数倍の空気を送るためイオン交
換膜中の水分が空気に持ち出されそのために膜が乾いて
くる。また固体高分子電解質型燃料電池は一般的に10
0℃付近の温度で運転されるために水分が蒸発してイオ
ン交換膜が乾くということもある。このために従来は適
量と計算される一定量の水蒸気を燃料ガスおよぴ/また
は酸化剤ガス中に補給して電池に送り込む方法を採用し
ている。水蒸気補給の一般的な方法としては所定温度に
維持されたバブラに反応ガスをバブリングする方法がと
られている。In such a solid polyelectrolyte fuel cell, protons move in a hydrated state as they move from the anode to the cathode in the ion exchange membrane, so that the water content near the anode decreases and ion exchange occurs. The film dries. Therefore, it becomes difficult for protons to move near the anode unless water is supplied. When air is used as the oxidant, several times the theoretical consumption of air is sent, and the moisture in the ion-exchange membrane is carried out to the air, which causes the membrane to dry. In addition, solid polymer electrolyte fuel cells generally have 10
Since the operation is performed at a temperature near 0 ° C., water may evaporate and the ion exchange membrane may dry. For this reason, conventionally, a method has been adopted in which a fixed amount of water vapor, which is calculated as an appropriate amount, is replenished in the fuel gas and / or the oxidant gas and sent to the battery. As a general method of supplying steam, a method of bubbling a reaction gas through a bubbler maintained at a predetermined temperature is used.
【0007】図2は従来の固体高分子電解質型燃料電池
を示す配置図である。固体高分子電解質膜2にアノード
1とカソード3が配置されセルが構成される。このセル
のアノード1には燃料ガスが供給される。セルのカソー
ド3には酸化剤ガスが供給される。燃料ガスと酸化剤ガ
スの両反応ガスはそれぞれの反応ガス供給系11、12
を通って供給される。反応ガス供給系にはそれぞれバブ
ラである加湿器5が設けられる。セルを通った両反応ガ
スはそれぞれの反応ガス排出系9、10を介して排出さ
れる。FIG. 2 is a layout view showing a conventional solid polymer electrolyte fuel cell. The anode 1 and the cathode 3 are arranged on the solid polymer electrolyte membrane 2 to form a cell. Fuel gas is supplied to the anode 1 of this cell. An oxidant gas is supplied to the cathode 3 of the cell. Both the reaction gas of the fuel gas and the oxidant gas are supplied to the respective reaction gas supply systems 11, 12
Supplied through. A humidifier 5 which is a bubbler is provided in each of the reaction gas supply systems. Both reaction gases that have passed through the cell are discharged through the respective reaction gas discharge systems 9 and 10.
【0008】[0008]
【発明が解決しようとする課題】しかしながら上述の従
来の方法にあっては反応ガスをバブラに一回通過させる
のみであり、水蒸気の反応ガスへの補給量が不足して長
時間の運転後には膜は乾燥状態となり電池性能が低下す
るという問題があった。乾燥状態になると膜の電気抵抗
が上昇してセルの特性が低下する。この発明は上述の点
に鑑みてなされその目的は反応ガス中に水蒸気を十分補
給するようにしてセル特性の低下がなく、信頼性に優れ
る固体高分子電解質型燃料電池を提供することにある。However, in the above-mentioned conventional method, the reaction gas is passed through the bubbler only once, and the amount of replenishment of steam to the reaction gas is insufficient, and after a long time operation, There is a problem that the film becomes dry and the battery performance is deteriorated. When it is in a dry state, the electric resistance of the film increases and the cell characteristics deteriorate. The present invention has been made in view of the above points, and an object thereof is to provide a solid polymer electrolyte fuel cell which is excellent in reliability by sufficiently supplementing water vapor into a reaction gas without deterioration of cell characteristics.
【0009】[0009]
【課題を解決するための手段】上述の目的はセルと、反
応ガス供給系と、反応ガス排出系と、加湿器と、リサイ
クルループとを有し、セルは固体高分子電解質膜にアノ
ードとカソードを配したものであり、反応ガス供給系は
加湿器を介してセルに反応ガスを供給するものであり、
反応ガス排出系はセルを通過した反応ガスを排出するも
のであり、リサイクルループは排出された反応ガス排出
系の反応ガスを再度セルに帰還させる回路であり、その
ループ内に加湿器を備え、加湿器は反応ガスに水蒸気を
加えるものであるとすることにより達成される。The above-mentioned object has a cell, a reaction gas supply system, a reaction gas discharge system, a humidifier, and a recycle loop, and the cell comprises a solid polymer electrolyte membrane, an anode and a cathode. The reaction gas supply system supplies reaction gas to the cell through a humidifier,
The reaction gas exhaust system is for exhausting the reaction gas that has passed through the cell, and the recycle loop is a circuit for returning the exhausted reaction gas of the reaction gas exhaust system to the cell again, and a humidifier is provided in the loop. The humidifier is achieved by adding steam to the reaction gas.
【0010】[0010]
【作用】リサイクルループを帰還する反応ガスは既に水
蒸気を含んでおり再度加湿器を通過させることにより反
応ガス中の水蒸気含有量を増加させることができる。The reaction gas returning to the recycle loop already contains water vapor, and the water vapor content in the reaction gas can be increased by passing it through the humidifier again.
【0011】[0011]
【実施例】次にこの発明の実施例を図面に基づいて説明
する。図1はこの発明の実施例に係る固体高分子電解質
型燃料電池を示す配置図である。従来の固体高分子電解
質型燃料電池を示す配置図とはリサイクルループ7、8
が設けられている点が異なる。各リサイクルループには
ポンプ4、6がそれぞれ設けられる。リサイクルする反
応ガスは加湿器5を通ってセルに導かれる。リサイクル
する反応ガスは加湿器を多数回通過するので水蒸気含有
量は大きくセルに対して必要量の水を補給することがで
きる。リサイクルする反応ガスの還流比はセルの出力特
性との関係で任意に設定することができる。Embodiments of the present invention will now be described with reference to the drawings. FIG. 1 is a layout view showing a solid polymer electrolyte fuel cell according to an embodiment of the present invention. The layout of the conventional solid polymer electrolyte fuel cell is different from the recycle loops 7 and 8.
Is different. Pumps 4 and 6 are provided in each recycling loop. The reaction gas to be recycled is introduced into the cell through the humidifier 5. Since the reaction gas to be recycled passes through the humidifier a number of times, it has a large water vapor content and can replenish the cell with a necessary amount of water. The reflux ratio of the reaction gas to be recycled can be arbitrarily set in relation to the output characteristics of the cell.
【0012】上述の例では加湿器にバブラを使用してい
るが、バブラの他水蒸気発生装置や超音波加湿器、内部
加湿器等もリサイクルループとともに使用することがで
きる。 また図示しないがセルの乾燥状態を検知する導
電率形の信号によりポンプ6または4を駆動して反応ガ
スのリサイクル量を制御すれば、セル内高分子電解質の
水分量を最適状態に維持することもできる。In the above example, a bubbler is used as the humidifier, but a steam generator, an ultrasonic humidifier, an internal humidifier, etc. can be used together with the recycle loop in addition to the bubbler. Further, although not shown, if the pump 6 or 4 is driven by a conductivity type signal for detecting the dry state of the cell to control the amount of recycled reaction gas, the amount of water in the polymer electrolyte in the cell can be maintained in an optimum state. Can also
【0013】[0013]
【発明の効果】セルと、反応ガス供給系と、反応ガス排
出系と、加湿器と、リサイクルループとを有し、セルは
固体高分子電解質膜にアノードとカソードを配したもの
であり、反応ガス供給系は加湿器を介してセルに反応ガ
スを供給するものであり、反応ガス排出系はセルを通過
した反応ガスを排出するものであり、リサイクルループ
は排出された反応ガス排出系の反応ガスを再度セルに帰
還させる回路であり、そのループ内に加湿器を備え、加
湿器は反応ガスに水蒸気を加えるものであるので固体高
分子電解質は常時湿潤状態に維持され安定した電池の運
転が可能となる。また本発明の電池では従来の電池に比
較してセルを通過する反応ガスの総量をより多くするこ
とができるので反応ガスの等配性を良くすることがで
き、さらにセル内部での温度分布をより小さくすること
ができる。The present invention has a cell, a reaction gas supply system, a reaction gas discharge system, a humidifier, and a recycle loop. The cell is a solid polymer electrolyte membrane with an anode and a cathode. The gas supply system supplies the reaction gas to the cell through the humidifier, the reaction gas discharge system discharges the reaction gas that has passed through the cell, and the recycle loop is the reaction of the discharged reaction gas discharge system. It is a circuit that returns gas to the cell again, and a humidifier is provided in the loop.Since the humidifier adds water vapor to the reaction gas, the solid polymer electrolyte is always kept in a wet state and stable battery operation is possible. It will be possible. Further, in the battery of the present invention, the total amount of the reaction gas passing through the cell can be made larger than that in the conventional battery, so that the equidistributed property of the reaction gas can be improved, and further the temperature distribution inside the cell can be improved. Can be smaller.
【図1】この発明の実施例に係る固体高分子電解質型燃
料電池を示す配置図FIG. 1 is a layout view showing a solid polymer electrolyte fuel cell according to an embodiment of the present invention.
【図2】従来の固体高分子電解質型燃料電池を示す配置
図FIG. 2 is a layout view showing a conventional solid polymer electrolyte fuel cell.
1 アノード 2 固体高分子電解質 3 カソード 4 ポンプ 5 加湿器 6 ポンプ 7 リサイクルループ 8 リサイクルループ 9 反応ガス排出系 10 反応ガス排出系 11 反応ガス供給系 12 反応ガス供給系 1 Anode 2 Solid Polymer Electrolyte 3 Cathode 4 Pump 5 Humidifier 6 Pump 7 Recycle Loop 8 Recycle Loop 9 Reactive Gas Exhaust System 10 Reactive Gas Exhaust System 11 Reactive Gas Supply System 12 Reactive Gas Supply System
Claims (3)
系と、加湿器と、リサイクルループとを有し、 セルは固体高分子電解質膜にアノードとカソードを配し
たものであり、 反応ガス供給系は加湿器を介してセルに反応ガスを供給
するものであり、 反応ガス排出系はセルを通過した反応ガスを排出するも
のであり、 リサイクルループは排出された反応ガス排出系の反応ガ
スを再度セルに帰還させる回路であり、そのループ内に
加湿器を備え、 加湿器は反応ガスに水蒸気を加えるものであることを特
徴とする固体高分子電解質型燃料電池。1. A cell comprising a cell, a reaction gas supply system, a reaction gas discharge system, a humidifier, and a recycle loop, wherein the cell comprises a solid polymer electrolyte membrane and an anode and a cathode. The gas supply system supplies the reaction gas to the cell via the humidifier, the reaction gas discharge system discharges the reaction gas that has passed through the cell, and the recycle loop the reaction of the discharged reaction gas discharge system. A solid polymer electrolyte fuel cell characterized in that it is a circuit for returning gas to the cell again, and a humidifier is provided in the loop, and the humidifier adds water vapor to the reaction gas.
はバブラであることを特徴とする固体高分子電解質型燃
料電池。2. The solid polymer electrolyte fuel cell according to claim 1, wherein the humidifier is a bubbler.
ス供給系の加湿器とリサイクルループ内の加湿器は同一
のものであることを特徴とする固体高分子電解質型燃料
電池。3. The solid polymer electrolyte fuel cell according to claim 1, wherein the humidifier in the reaction gas supply system and the humidifier in the recycle loop are the same.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3252637A JPH0594832A (en) | 1991-10-01 | 1991-10-01 | Solid high molecular electrolyte type fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3252637A JPH0594832A (en) | 1991-10-01 | 1991-10-01 | Solid high molecular electrolyte type fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0594832A true JPH0594832A (en) | 1993-04-16 |
Family
ID=17240123
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3252637A Pending JPH0594832A (en) | 1991-10-01 | 1991-10-01 | Solid high molecular electrolyte type fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0594832A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06231788A (en) * | 1993-02-03 | 1994-08-19 | Matsushita Electric Ind Co Ltd | Solid high polymer type fuel cell |
JPH0714597A (en) * | 1993-06-07 | 1995-01-17 | Daimler Benz Ag | Method and equipment for humidifying process gas for operation of fuel cell device |
US6124052A (en) * | 1997-07-11 | 2000-09-26 | Kabushiki Kaisha Toyoda Jidoshokki Seisakusho | Solid polymer electrolyte fuel cell system |
EP1095414A4 (en) * | 1998-05-19 | 2001-09-19 | Int Fuel Cells Llc | System and method of water management in the operation of a fuel cell |
JP2002184439A (en) * | 2000-10-05 | 2002-06-28 | Honda Motor Co Ltd | Fuel cell system |
KR20030010236A (en) * | 2001-07-26 | 2003-02-05 | 현대자동차주식회사 | Fuel cell stack structure |
WO2004062016A1 (en) * | 2002-12-26 | 2004-07-22 | Sony Corporation | Hydrogen gas humidity controller, fuel cell, hydrogen gas humidity controlling method, and humidity controlling method of fuel cell |
KR100486561B1 (en) * | 2002-06-21 | 2005-05-03 | 엘지전자 주식회사 | Hydrogen gas recycling fuel cell |
JP2005259547A (en) * | 2004-03-12 | 2005-09-22 | Kemitsukusu:Kk | Fuel cell and its driving system |
JP2010016006A (en) * | 2009-10-21 | 2010-01-21 | Mitsubishi Heavy Ind Ltd | Polymer electrolyte fuel cell system |
-
1991
- 1991-10-01 JP JP3252637A patent/JPH0594832A/en active Pending
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06231788A (en) * | 1993-02-03 | 1994-08-19 | Matsushita Electric Ind Co Ltd | Solid high polymer type fuel cell |
JPH0714597A (en) * | 1993-06-07 | 1995-01-17 | Daimler Benz Ag | Method and equipment for humidifying process gas for operation of fuel cell device |
US6124052A (en) * | 1997-07-11 | 2000-09-26 | Kabushiki Kaisha Toyoda Jidoshokki Seisakusho | Solid polymer electrolyte fuel cell system |
EP1095414A4 (en) * | 1998-05-19 | 2001-09-19 | Int Fuel Cells Llc | System and method of water management in the operation of a fuel cell |
JP2002518791A (en) * | 1998-05-19 | 2002-06-25 | インターナショナル フューエル セルズ コーポレイション | Control device and control method of water in operation of fuel cell |
JP2002184439A (en) * | 2000-10-05 | 2002-06-28 | Honda Motor Co Ltd | Fuel cell system |
KR20030010236A (en) * | 2001-07-26 | 2003-02-05 | 현대자동차주식회사 | Fuel cell stack structure |
KR100486561B1 (en) * | 2002-06-21 | 2005-05-03 | 엘지전자 주식회사 | Hydrogen gas recycling fuel cell |
WO2004062016A1 (en) * | 2002-12-26 | 2004-07-22 | Sony Corporation | Hydrogen gas humidity controller, fuel cell, hydrogen gas humidity controlling method, and humidity controlling method of fuel cell |
JP2005259547A (en) * | 2004-03-12 | 2005-09-22 | Kemitsukusu:Kk | Fuel cell and its driving system |
JP2010016006A (en) * | 2009-10-21 | 2010-01-21 | Mitsubishi Heavy Ind Ltd | Polymer electrolyte fuel cell system |
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