JPH06124722A - Heating and humidifying device and fuel cell - Google Patents

Heating and humidifying device and fuel cell

Info

Publication number
JPH06124722A
JPH06124722A JP4271855A JP27185592A JPH06124722A JP H06124722 A JPH06124722 A JP H06124722A JP 4271855 A JP4271855 A JP 4271855A JP 27185592 A JP27185592 A JP 27185592A JP H06124722 A JPH06124722 A JP H06124722A
Authority
JP
Japan
Prior art keywords
heating
water
humidifying
fuel cell
cooling water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP4271855A
Other languages
Japanese (ja)
Inventor
Katsuo Hashizaki
克雄 橋崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP4271855A priority Critical patent/JPH06124722A/en
Publication of JPH06124722A publication Critical patent/JPH06124722A/en
Pending legal-status Critical Current

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04119Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04029Heat exchange using liquids
    • 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

Landscapes

  • Fuel Cell (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)

Abstract

PURPOSE:To enable a heating and humidifying device to be made compact, allow the arbitrary setting of an applied humidity amount within saturated vapor pressure, depending upon a change in the number of stacks, and further enable differential pressure to be enlarged between gas and cooling water sides via the application of a polymer film. CONSTITUTION:This device is characteristic in that gas and cooling water as turned into hot water state for applying heat and humidity, are respectively introduced to both sides of polymer films 44 and 45, and the films 44 and 45 or porous body is made to absorb the hot water. Also, the device is characteristic in that the absorbed water is vaporized into the gas for heat and humidity application on the other side of the body, or humidity is applied thereto concurrently via the heat of the hot water. Furthermore, the device is characteristic in that the device is integrally stacked on a fuel cell body having an electrode joint body with electrodes laid at both side of a solid electrolyte, and a fuel cell body with separators laid at both sides of the body.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、加温・加湿システム装
置及びこの装置と燃料電池本体を一体化させた燃料電池
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating / humidifying system device and a fuel cell in which the device is integrated with a fuel cell body.

【0002】[0002]

【従来の技術】周知の如く、固体高分子電解質燃料電池
の発電原理は図1に示す通りである。電極接合体1は、
電解質(イオン交換膜)2としてフッ素樹脂系の高分子
イオン交換膜(例えば、スルホン酸基を持つフッ素樹脂
系イオン交換膜)を用い、これを中央にして両面に例え
ば白金からなる触媒電極(負極)3,触媒電極(陽極)
4を付着させ、更にその両面をポーラスなカーボン電極
(負極)5,カーボン電極(陽極)6でサンドイッチ状
に挟み重ねた構成となっている。
2. Description of the Related Art As is well known, the power generation principle of a solid polymer electrolyte fuel cell is as shown in FIG. The electrode assembly 1 is
As the electrolyte (ion exchange membrane) 2, a fluororesin polymer ion exchange membrane (for example, a fluororesin ion exchange membrane having a sulfonic acid group) is used, and a catalyst electrode (negative electrode) made of, for example, platinum on both sides with this as the center. ) 3, catalyst electrode (anode)
4 is attached, and both surfaces thereof are sandwiched between porous carbon electrodes (negative electrode) 5 and carbon electrode (anode) 6 and stacked.

【0003】燃料として供給された水素は、触媒電極3
上で水素イオン化され、水素イオンは電解質2中をH+
・H2 Oとして陽極へ向かって移動する。
Hydrogen supplied as fuel is used as a catalyst electrode 3
The hydrogen ions are ionized above, and the hydrogen ions are H + in the electrolyte 2.
・ Move toward the anode as H 2 O.

【0004】触媒電極4上で酸化剤として供給された酸
素又は空気中の酸素及び外部回路7を流通してきた電子
と反応し、水を生成,排出される。この時、外部回路7
を流通してきた電子の流れが直流の電気エネルギーとし
て利用できる。
On the catalyst electrode 4, oxygen supplied as an oxidant or oxygen in the air and the electrons flowing through the external circuit 7 react with each other to generate and discharge water. At this time, the external circuit 7
The flow of electrons that has flowed through can be used as direct-current electrical energy.

【0005】電解質2となるイオン交換膜において、前
述のような水素イオン透過性を実現させるためには、イ
オン交換膜を常に十分なる保水状態に保持し続ける必要
がある。イオン交換膜は乾燥状態になると水素イオン透
過性が低減し、燃料電池としてはその電気抵抗が大きく
なり発電不可能な状況に陥いる。
In order to realize the above-mentioned hydrogen ion permeability in the ion exchange membrane serving as the electrolyte 2, it is necessary to always keep the ion exchange membrane in a sufficient water retention state. When the ion-exchange membrane is in a dry state, its hydrogen ion permeability is reduced, and the electric resistance of the fuel cell becomes large, which makes it impossible to generate electricity.

【0006】電解質2となるイオン交換膜の保水状態を
保つために、通常燃料として供給される水素又は酸化剤
として供給される酸素又は空気、あるいは両者を燃料電
池の運転温度である80℃前後まで加温し、その温度に
おける飽和水蒸気分圧相当の水蒸気で加湿させた水素,
酸素又は空気として電極接合体1に供給し、電解質2で
あるイオン交換膜の保水状態を保持し続けるようにして
いる。以下に、図1の燃料電池における負極側,陽極側
等の化学反応式を示す。
In order to maintain the water-retaining state of the ion exchange membrane serving as the electrolyte 2, hydrogen, which is usually supplied as a fuel, oxygen or air, which is supplied as an oxidant, or both are used up to around 80 ° C. which is the operating temperature of the fuel cell. Hydrogen that has been heated and moistened with steam equivalent to saturated steam partial pressure at that temperature,
Oxygen or air is supplied to the electrode assembly 1 so that the water exchange state of the ion exchange membrane, which is the electrolyte 2, is maintained. The chemical reaction formulas on the negative electrode side and the positive electrode side in the fuel cell of FIG. 1 are shown below.

【0007】 負極側: H2 →2H+ +2e- 陽極側: (1/2)O2 +2H+ +2e- →H2 O 全反応: H2 +(1/2) O2 →H2 O また、従来の固体高分子電解質燃料電池の加湿・加湿シ
ステム装置,即ち気体燃料である水素,気体酸化剤であ
る酸素又は空気,この両者を加温・加湿して燃料電池へ
供給する加温・加湿システム装置は、図2に示す通りで
ある。なお、図2では、両者を加温・加湿しているが、
水素のみあるいは酸素又は空気のみを本システム装置に
より加温・加湿する場合もある。
Negative electrode side: H 2 → 2H + + 2e Anode side: (1/2) O 2 + 2H + + 2e → H 2 O Total reaction: H 2 + (1/2) O 2 → H 2 O Humidification / humidification system device for a conventional solid polymer electrolyte fuel cell, that is, a heating / humidification system for supplying hydrogen to a fuel cell by heating / humidifying hydrogen, which is a gaseous fuel, oxygen or air, which is a gaseous oxidizer. The device is as shown in FIG. In addition, although both are heated and humidified in FIG.
In some cases, only hydrogen, oxygen, or air is heated and humidified by this system device.

【0008】水素、酸素又は空気を電気ヒータ11で燃料
電池の運転温度と略同等の温度40℃前後から100℃
前後に加温された純水12中を通過させることにより、水
素、酸素又は空気は飽和蒸気圧分相当に充分加湿させる
ことができる。この充分に加湿させられた水素、酸素又
は空気を燃料電池本体13に供給することにより、電解質
2であるイオン交換膜に水分が常に供給され、保水状態
を保持し続けることが可能となる。なお、燃料電池本体
13の冷却水を加温・加湿装置14,15に導き、その温水を
加温・加湿水源として利用することも可能である。
Hydrogen, oxygen or air is supplied to the electric heater 11 at a temperature substantially equal to the operating temperature of the fuel cell from about 40 ° C. to 100 ° C.
By passing through the pure water 12 heated before and after, hydrogen, oxygen, or air can be sufficiently humidified corresponding to the saturated vapor pressure. By supplying the sufficiently humidified hydrogen, oxygen or air to the fuel cell main body 13, water is constantly supplied to the ion exchange membrane which is the electrolyte 2, and it becomes possible to maintain the water retention state. The fuel cell body
It is also possible to guide 13 cooling water to the heating / humidifying devices 14 and 15 and use the hot water as a source of heating / humidifying water.

【0009】[0009]

【発明が解決しようとする課題】しかしながら、従来の
加温・加湿システム装置は以下の課題を有する。
However, the conventional heating / humidifying system device has the following problems.

【0010】(1) 加温・加湿装置(燃料側)14,加温・
加湿装置(酸化剤側)15として純水12の小型容器が必要
であり、コンパクト性に欠ける。
(1) Heating / humidifying device (fuel side) 14, heating /
A compact container of pure water 12 is required as the humidifier (oxidizer side) 15, which lacks compactness.

【0011】(2) 加湿量を外部からの電気ネルギー(例
えば電気ヒータ11)等を利用した温度調整でしか制御で
きない。
(2) The amount of humidification can be controlled only by temperature adjustment using electric energy (for example, electric heater 11) from the outside.

【0012】(3) 電気ヒータ11等、制御項目が多くな
り、システム全体が複雑となる。
(3) The number of control items such as the electric heater 11 increases, and the entire system becomes complicated.

【0013】(4) 圧力をもった気体を加温・加湿させる
場合、容器の耐圧性を配慮せねばならず、設計が複雑と
なる。
(4) When heating and humidifying a gas having a pressure, the pressure resistance of the container must be taken into consideration, which complicates the design.

【0014】この発明はこうした事情を考慮してなされ
たもので、高分子膜又は多孔質板を利用した気体の加温
・加湿システムを利用することにより加温・加湿装置を
コンパクト化でき、かつ加湿量を積層数の変化により飽
和蒸気圧の範囲で任意に設定でき、更に高分子膜の採用
により気体側と冷却水側の差圧を大きくとることが可能
な加温・加湿システム装置及び燃料電池を提供すること
を目的とする。
The present invention has been made in consideration of such circumstances, and the heating / humidifying device can be made compact by using a gas heating / humidifying system using a polymer membrane or a porous plate, and The amount of humidification can be set arbitrarily within the range of saturated vapor pressure by changing the number of stacks, and the adoption of a polymer membrane can increase the pressure difference between the gas side and the cooling water side. The purpose is to provide a battery.

【0015】[0015]

【課題を解決するための手段】本願第1の発明は、高分
子膜又は水を透過できる多孔質体の両面に、加温・加湿
させる気体、及び温水となった冷却水を夫々導き、前記
温水を高分子膜又は多孔質体に吸水させ、その吸水した
水を他方の面の加温・加湿させる気体中に蒸発させる
か、あるいは温水の持つ熱により同時に加湿させること
を特徴とする加温・加湿システム装置である。
According to a first aspect of the present invention, a gas for heating / humidifying and cooling water that has become hot water are introduced to both sides of a polymer membrane or a porous body permeable to water, respectively. A heating method characterized in that hot water is absorbed by a polymer membrane or a porous body, and the absorbed water is evaporated into a gas on the other surface for heating and humidifying, or is simultaneously heated by the heat of the hot water. -It is a humidification system device.

【0016】本願第2の発明は、固体高分子電解質の両
側に電極を夫々配置した電極接合体と該電極接合体の両
側に配置したセパレータとを有する燃料電池本体に、請
求項2記載の加温・加湿システム装置を一体に積層した
ことを特徴とする燃料電池である。
According to a second aspect of the present invention, there is provided a fuel cell main body having an electrode assembly in which electrodes are arranged on both sides of a solid polymer electrolyte and a separator arranged in both sides of the electrode assembly. A fuel cell is characterized in that a temperature / humidification system device is integrally laminated.

【0017】図3は、この発明に係る高分子膜(例え
ば、スルホン酸基を持つフッ素樹脂系イオン交換膜)を
利用した気体の加温・加湿システム装置の原理図を示
す。図中の21は中央に配置された高分子膜を示し、両側
に気体(例えば、水素、酸素又は空気)、及び排熱等を
回収し温水となった燃料電池本体の冷却水を導くように
なっている。
FIG. 3 shows a principle diagram of a gas heating / humidification system device using a polymer membrane (for example, a fluororesin ion exchange membrane having a sulfonic acid group) according to the present invention. Reference numeral 21 in the figure denotes a polymer membrane arranged in the center, and guides the gas (for example, hydrogen, oxygen or air) and the cooling water of the fuel cell main body which has become hot water by collecting exhaust heat and the like on both sides. Has become.

【0018】図4(A),(B)は、高分子膜21を利用
した加温・加湿システム装置の概略構成図を示し、図4
(A)は上面図、図4(B)は同図(A)の側面図であ
る。図中の22,23は、高分子膜21の両側に配置された第
1セパレータ(加温・加湿気体側),第2セパレータ
(冷却水側)を示す。これらのセパレータ22,23の材質
は、カーボン製又は金属製である。前記高分子側21の第
1セパレータ22には、加温・加湿させたい気体(例え
ば、水素、酸素又は空気)を導く加温・加湿気体流路溝
24が設けられている。前記高分子側21の第2セパレータ
23には、温水となった冷却水を導く冷却水流路溝25が設
けられている。
FIGS. 4 (A) and 4 (B) are schematic configuration diagrams of a heating / humidifying system device using the polymer film 21, and FIG.
4A is a top view, and FIG. 4B is a side view of FIG. Reference numerals 22 and 23 in the figure denote a first separator (heated / humidified body side) and a second separator (cooling water side), which are arranged on both sides of the polymer film 21, respectively. The material of these separators 22 and 23 is carbon or metal. The first separator 22 on the polymer side 21 has a heating / humidifying body channel groove for guiding a gas (eg, hydrogen, oxygen or air) to be heated / humidified.
24 are provided. Second separator on the polymer side 21
The cooling water passage groove 25 that guides the cooling water that has become hot water is provided in the 23.

【0019】なお、前記加温・加湿気体流路溝24、冷却
水流路溝25の代りに、気体,冷却水を高分子膜21の両面
に導入する方法として、ポーラスなカーボン板で高分子
膜21を挟み、その空隙中を気体,冷却水を通過させるこ
とにより、加温・加湿させることも可能である。
As a method of introducing gas and cooling water into both sides of the polymer film 21 instead of the heating / humidifying body flow path groove 24 and the cooling water flow path groove 25, a polymer film made of a porous carbon plate is used. It is also possible to heat and humidify by sandwiching 21 and passing gas and cooling water through the gap.

【0020】図5は、この発明に係る水の透過できる多
孔質体(例えば、セラミック板,カーボン板)を利用し
た気体の加温・加湿システム装置の原理図を示す。図中
の31は中央に配置された多孔質体を示し、両側に気体
(例えば、水素、酸素又は空気)、及び排熱等を回収し
温水となった燃料電池本体の冷却水を導くようになって
いる。
FIG. 5 shows a principle diagram of a gas heating / humidification system device using a porous body (for example, a ceramic plate or a carbon plate) which can permeate water according to the present invention. Reference numeral 31 in the figure denotes a porous body arranged in the center, and guides the gas (for example, hydrogen, oxygen or air) and the cooling water of the fuel cell body that has become hot water by collecting exhaust heat and the like on both sides. Has become.

【0021】図6(A),(B)は、多孔質体31を利用
した加温・加湿システム装置の概略構成図を示し、図6
(A)は上面図、図6(B)は同図(A)の側面図であ
る。図中の32,33は、多孔質体31の両側に配置された第
1セパレータ(加温・加湿気体側),第2セパレータ
(冷却水側)を示す。これらのセパレータ32,33の材質
は、カーボン又は金属製である。前記高分子側31の第1
セパレータ32には、加温・加湿させたい気体(例えば、
水素、酸素又は空気)を導く加温・加湿気体流路溝34が
設けられている。前記高分子側31の第2セパレータ32に
は、温水となった冷却水を導く冷却水流路溝35が設けら
れている。
FIGS. 6 (A) and 6 (B) are schematic configuration diagrams of a heating / humidifying system device using the porous body 31, and FIG.
6A is a top view, and FIG. 6B is a side view of FIG. Reference numerals 32 and 33 in the figure denote a first separator (heated / humidified body side) and a second separator (cooling water side) arranged on both sides of the porous body 31. The material of these separators 32, 33 is carbon or metal. First of the polymer side 31
The separator 32 includes a gas to be heated / humidified (for example,
A heating / humidifying body flow path groove 34 for guiding hydrogen, oxygen, or air) is provided. The second separator 32 on the polymer side 31 is provided with a cooling water flow channel groove 35 for guiding the cooling water that has become hot water.

【0022】図7(A),(B)は、溝付き多孔質体36
を利用した加温・加湿システム装置の概略構成図を示
し、図7(A)は上面図、図7(B)は同図(A)の側
面図である。図中の37,38は、それぞれ前記多孔質体36
の両側に配置された第1セパレータ(加温・加湿気体
側),第2セパレータ(冷却水側)を示す。これらのセ
パレータ37,38の材質は、カーボン製又は金属製であ
る。前記第1セパレータ37側の前記多孔質体36には、加
温・加湿させたい気体(例えば、水素、酸素又は空気)
を導く加温・加湿気体流路溝39が設けられている。第2
セパレータ38側の前記多孔質体36には、温水となった冷
却水を導く冷却水流路溝40が設けられている。
FIGS. 7A and 7B show a porous body 36 with grooves.
7A and 7B are schematic configuration diagrams of a heating / humidifying system device utilizing the above, FIG. 7A is a top view, and FIG. 7B is a side view of FIG. 37 and 38 in the figure are the porous bodies 36, respectively.
The first separator (on the heating / humidifying body side) and the second separator (on the cooling water side) arranged on both sides of the above are shown. The material of these separators 37, 38 is carbon or metal. The porous body 36 on the side of the first separator 37 has a gas (for example, hydrogen, oxygen or air) to be heated / humidified.
There is provided a heating / humidifying body flow path groove 39 for guiding the heat. Second
The porous body 36 on the separator 38 side is provided with a cooling water flow channel groove 40 that guides cooling water that has become hot water.

【0023】[0023]

【作用】本発明に係る加温・加湿システム装置の作用
は、次に述べる通りである。
The operation of the heating / humidifying system device according to the present invention is as described below.

【0024】図3,図4の高分子膜を利用した気体の加
温・加湿システム装置の場合、高分子膜21を挟み、その
両側に加温・加湿させる気体、排熱等を回収し温水とな
った冷却水を導くことにより、温水は高分子膜21に吸水
され、その吸水された水は他面の加温・加湿させたい気
体中に蒸発、又は温水の持つ熱により同時に加温させる
ことも可能であり、本原理を利用することで同時に加温
・加湿システムを構成させることが可能である。また、
図4のように、第1セパレータ22,高分子膜21及び第2
セパレータ23を積層した構成とし、加温・加湿気体流路
溝24を通過する流速を調整することにより、加湿量を飽
和蒸気圧分圧の範囲内で任意に調整できる。
In the case of the gas heating / humidifying system device using the polymer membrane shown in FIGS. 3 and 4, the polymer membrane 21 is sandwiched and the gas to be heated / humidified, exhaust heat, etc. are collected on both sides of the polymer membrane 21 to obtain hot water. The hot water is absorbed by the polymer film 21 by introducing the cooled water, and the absorbed water evaporates in the gas to be heated / humidified on the other surface or is simultaneously heated by the heat of the hot water. It is also possible to use this principle to simultaneously configure a heating / humidifying system. Also,
As shown in FIG. 4, the first separator 22, the polymer film 21, and the second
By configuring the separators 23 to be laminated and adjusting the flow rate passing through the heating / humidifying body flow path grooves 24, the humidification amount can be arbitrarily adjusted within the range of the saturated vapor pressure partial pressure.

【0025】図5,図6及び図7の多孔質体を利用した
気体の加温・加湿システム装置の場合、水の多孔質体を
中央に配置し、その両側に加温・加湿させる気体(例え
ば、水素,酸素又は空気)、排熱等を回収し終った温水
を導くことにより、温水は多孔質体中に給水,含水さ
れ、多面の加温・加湿させたい気体中に蒸発,又は温水
の持つ熱により同時に加温させることも可能であり、本
原理を利用することで同時に加温・加湿システムを構成
させることが可能である。図6,図7は気体を温水を多
孔質体に導く一例を示すが、第1セパレータ,高分子膜
及び第2セパレータを積層した構成とし、加温・加湿気
体流路溝を通過する流速を調整することにより、加湿量
を飽和蒸気圧分圧の範囲内で任意に調整できる。
In the case of the gas heating / humidifying system device using the porous body shown in FIGS. 5, 6 and 7, the porous body of water is arranged at the center and the gas to be heated / humidified on both sides thereof ( (For example, hydrogen, oxygen or air), by introducing hot water that has recovered exhaust heat, etc., the hot water is supplied to the porous body and contains water, which evaporates or warms water into the gas to be heated / humidified on multiple sides. It is also possible to simultaneously heat the same with the heat of the, and by using this principle, it is possible to configure a heating / humidifying system at the same time. 6 and 7 show an example of introducing hot water into the porous body by gas, the first separator, the polymer membrane and the second separator are laminated, and the flow velocity through the heating / humidifying body flow channel is By adjusting, the amount of humidification can be arbitrarily adjusted within the range of the saturated vapor pressure partial pressure.

【0026】[0026]

【実施例】以下、この発明の実施例を図面を参照して説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0027】(実施例1)図8を参照する。図中の41,
42,43は、それぞれ第1セパレータ(水素用),第2セ
パレータ(冷却水/酸素又は空気用)及び第3セパレー
タ(冷却水用)である。ここで、各セパレータの材質
は、カーボン製又は金属製である。前記第1セパレータ
41と第2セパレータ42間には第1高分子膜44が配置さ
れ、第2セパレータ42と第3セパレータ43間には第2高
分子膜45が配置されている。ここで、各高分子膜の材質
は、スルホン酸基を持つフッ素樹脂系イオン交換膜であ
る。なお、前記第1〜3セパレータの主面を、便宜上、
図の左側から順にA面,B面,C面,D面,E面と呼
ぶ。
(Example 1) Referring to FIG. 41 in the figure
42 and 43 are a first separator (for hydrogen), a second separator (for cooling water / oxygen or air), and a third separator (for cooling water), respectively. Here, the material of each separator is carbon or metal. The first separator
A first polymer film 44 is arranged between 41 and the second separator 42, and a second polymer film 45 is arranged between the second separator 42 and the third separator 43. Here, the material of each polymer membrane is a fluororesin ion exchange membrane having a sulfonic acid group. In addition, the main surface of the first to third separators, for convenience,
The planes A, B, C, D, and E are referred to in this order from the left side of the drawing.

【0028】前記第1セパレータ41のB面(第1高分子
膜44側)には、水素を導く第1水素流路46が設けられて
いる。前記第2セパレータ42のC面(第1高分子膜44
側)には、(燃料電池より)温水となった冷却水を導く
第1冷却水流路(水素用)47が設けられている。前記第
2セパレータ42のD面(第2高分子膜45側)には、酸素
又は空気を導く第1酸素又は空気流路48が設けられてい
る。前記第3セパレータ43のE面(第3高分子膜45側)
には、第2冷却水流路(酸素又は空気用)49が設けられ
ている。前記第1水素流路46と第1冷却水流路47は第1
高分子膜44を挟んだ合わせ面(B−C面)で直交するよ
うに配置され、前記第1酸素又は空気流路48と第2冷却
水流路49は第2高分子膜45を挾んだ合わせ面(D−E
面)で直交するように配置されている。
A first hydrogen flow path 46 for introducing hydrogen is provided on the surface B (on the side of the first polymer film 44) of the first separator 41. The C surface of the second separator 42 (the first polymer film 44
On the side), a first cooling water channel (for hydrogen) 47 for guiding the cooling water that has become hot water (from the fuel cell) is provided. A first oxygen or air flow path 48 for guiding oxygen or air is provided on the D surface (on the side of the second polymer film 45) of the second separator 42. E surface of the third separator 43 (the third polymer film 45 side)
A second cooling water channel (for oxygen or air) 49 is provided in the. The first hydrogen flow path 46 and the first cooling water flow path 47 are the first
The first oxygen or air passage 48 and the second cooling water passage 49 are arranged so as to be orthogonal to each other on the mating planes (B-C planes) sandwiching the polymer membrane 44, and the second polymer membrane 45 is sandwiched between them. Mating surface (D-E
They are arranged so that they are orthogonal to each other.

【0029】こうした構成の加温・加湿システム装置に
おいて、例えば固体高分子電解質燃料電池に供給される
水素は第1セパレータ41のA面より導入され、第1セパ
レータ41のB面へ供給される。一方、酸素又は空気は第
1セパレータ41のA面より導入され、第2セパレータ42
のD面へ供給される。前記水素は、第1セパレータ41の
B面上を第1高分子膜44に沿って分岐,流れるようにな
っている。また、酸素又は空気は、第2セパレータ42の
D面上を第2高分子膜45に沿って分岐,流れるようにな
っている。
In the heating / humidifying system device having such a structure, for example, hydrogen supplied to the solid polymer electrolyte fuel cell is introduced from the A surface of the first separator 41 and supplied to the B surface of the first separator 41. On the other hand, oxygen or air is introduced from the A side of the first separator 41, and the second separator 42
It is supplied to the D side of. The hydrogen is branched and flows on the B surface of the first separator 41 along the first polymer film 44. Further, oxygen or air branches and flows on the D surface of the second separator 42 along the second polymer film 45.

【0030】また、固体高分子電解質燃料電池の排熱を
回収して温水(80℃程度)となった冷却水は、第1セ
パレータ41のA面より導入され、第2セパレータ42のC
面及び第3セパレータ43のE面へ分岐,供給される。C
面,E面に分岐,供給された温水は、各々第1高分子膜
44,第2高分子膜45を介し、水素、酸素又は空気を加温
・加湿し、加温・加湿し終った温水は再び集められ、第
1セパレータ41より取出すことが可能となる。なお、加
湿量は、本構造を積層化することにより、飽和水蒸気分
圧の範囲内で任意に調整される。
Further, the cooling water which has recovered the exhaust heat of the solid polymer electrolyte fuel cell into hot water (about 80 ° C.) is introduced from the A side of the first separator 41, and the C of the second separator 42.
Surface and the E surface of the third separator 43 are branched and supplied. C
The hot water branched and supplied to the surface E and the surface E are respectively the first polymer film.
44, via the second polymer film 45, hydrogen, oxygen or air is heated and humidified, and the warm water that has been heated and humidified is collected again and can be taken out from the first separator 41. The amount of humidification can be arbitrarily adjusted within the range of saturated water vapor partial pressure by stacking this structure.

【0031】上記実施例1に係る加温・加湿システム装
置は、第1セパレータ41,第2セパレータ42及び第3セ
パレータ43間に夫々第1高分子膜44,第2高分子膜45を
配置して積層し、前記第1高分子膜44の両面には水素,
温水となった冷却水を夫々導き、第2高分子膜45の両面
には酸素又は空気,温水となった冷却水を夫々導く構成
になっているため、加温・加湿装置をコンパクト化で
き、かつ加湿量を積層数の変化により飽和蒸気圧の範囲
で任意に設定でき、更に高分子膜の採用により気体側と
冷却水側の差圧を大きくとることができる。
In the heating / humidifying system device according to the first embodiment, the first polymer film 44 and the second polymer film 45 are arranged between the first separator 41, the second separator 42 and the third separator 43, respectively. Hydrogen on both sides of the first polymer film 44,
Since the cooling water that has become hot water is guided respectively, and oxygen or air and the cooling water that has become hot water are respectively guided to both surfaces of the second polymer film 45, the heating / humidifying device can be made compact, In addition, the amount of humidification can be arbitrarily set within the range of saturated vapor pressure by changing the number of laminated layers, and by adopting a polymer membrane, the pressure difference between the gas side and the cooling water side can be made large.

【0032】(実施例2)この実施例2は、図8の場合
と比べ、第1高分子膜44を第1多孔質板とし、第2高分
子膜45を第2多孔質板に変わる点を除いて、実施例1の
場合と構成,作用が同じである。
(Example 2) Compared to the case of FIG. 8, this Example 2 uses the first polymer film 44 as the first porous plate and the second polymer film 45 as the second porous plate. Except for the above, the configuration and operation are the same as in the case of the first embodiment.

【0033】この実施例2によれば、上記実施例と同
様、加温・加湿装置のコンパクト化を実現でき、加湿量
を積層数の変化により飽和蒸気圧の範囲で任意に設定で
き、更に多孔質板の採用により気体側と冷却水側の差圧
を大きくとることができる。
According to the second embodiment, as in the above embodiment, the heating / humidifying device can be made compact, and the amount of humidification can be arbitrarily set within the range of saturated vapor pressure by changing the number of laminated layers. By adopting a quality plate, a large pressure difference between the gas side and the cooling water side can be secured.

【0034】(実施例3)図7を参照する。但し、図8
と同部材は同符号を付して説明を省略する。また、各セ
パレータ41〜43と各高分子膜44,45を積層した積層体
を、便宜上加温・加湿部51と呼ぶ。
(Embodiment 3) Referring to FIG. However, FIG.
The same members as and are denoted by the same reference numerals, and description thereof will be omitted. In addition, a laminated body in which the separators 41 to 43 and the polymer films 44 and 45 are laminated is referred to as a heating / humidifying section 51 for convenience.

【0035】図中の52は前記加温・加湿部51と一体化さ
れる燃料電池本体部であり、電極接合体53と両サイドの
第3セパレータ54,第4セパレータ55とから構成され
る。これらのセパレータ54,55の材質は、カーボン製又
は金属製である。前記電極接合体53側の第4セパレータ
54の主面(G面)には、第2水素流路56が設けられてい
る。前記電極接合体53側の第5セパレータ55の主面(H
面)には第2酸素又は空気流路57が設けられ、H面と反
対側の第5セパレータ55の主面(I面)には第3冷却水
流路58が設けられている。前記水素流路56と酸素又は空
気流路57は、電極接合体53を挾んだ合わせ面(G−H
面)で直交するように配置されている。
Reference numeral 52 in the figure denotes a fuel cell main body which is integrated with the heating / humidifying section 51, and is composed of an electrode assembly 53, a third separator 54 and a fourth separator 55 on both sides. The material of these separators 54, 55 is carbon or metal. Fourth separator on the side of the electrode assembly 53
A second hydrogen flow path 56 is provided on the main surface (G surface) of 54. The main surface of the fifth separator 55 on the side of the electrode assembly 53 (H
The second oxygen or air flow path 57 is provided on the surface), and the third cooling water flow path 58 is provided on the main surface (I surface) of the fifth separator 55 opposite to the H surface. The hydrogen flow path 56 and the oxygen or air flow path 57 are formed on the mating surface (GH) sandwiching the electrode assembly 53.
They are arranged so that they are orthogonal to each other.

【0036】こうした構成の燃料電池において、燃料で
ある水素(加温・加湿前)、酸化剤である酸素又は空気
(加温・加湿前)は、各々燃料電池本体52の第4セパレ
ータ54のF面の2ケの両隅の穴より導入し、加温・加湿
部51へ直接導入される。又、冷却水は第4セパレータ54
のF面のもう一隅の穴より導入し、第5セパレータ55の
I面でG−H面で起る電池反応の発熱を吸収し、温水と
なった後同じく加温・加湿部51へ導入される。
In the fuel cell having such a configuration, hydrogen (before heating / humidification) as a fuel and oxygen or air (before heating / humidification) as an oxidant are respectively generated in the F of the fourth separator 54 of the fuel cell main body 52. It is introduced from the holes at the two corners of the surface and directly introduced into the heating / humidifying section 51. Also, the cooling water is the fourth separator 54.
It is introduced from the hole at the other corner of the F surface of the fifth separator 55, absorbs the heat generated by the battery reaction occurring on the GH surface on the I surface of the fifth separator 55, and is introduced into the heating / humidifying section 51 after becoming hot water. It

【0037】加温・加湿部51へ導入された水素,酸素又
は空気は、湿水となった冷却水と第1・第2高分子膜4
4,45を挟み、互いに直交するように流される。ここ
で、冷却水(温水)の一部は第1・第2高分子膜44,45
に吸湿され、更に対面流れる水素,酸素又は空気宙に水
蒸気分圧差により蒸発していく。なお、加湿量は、燃料
電池運転温度における飽和水蒸気分圧の範囲内で、この
第1・第2高分子膜44,45を挟み同一構造を必要に応じ
積層することで可能である。
Hydrogen, oxygen, or air introduced into the heating / humidifying section 51 is the cooling water that has become wet water and the first and second polymer films 4
It is flown so that it sandwiches 4, 45 and is orthogonal to each other. Here, part of the cooling water (warm water) is the first and second polymer films 44, 45.
It is absorbed by the water, and then vaporizes in the facing hydrogen, oxygen or air due to the partial pressure difference of water vapor. The amount of humidification can be set within the range of the saturated water vapor partial pressure at the fuel cell operating temperature by stacking the same structure with the first and second polymer membranes 44 and 45 sandwiched therebetween, if necessary.

【0038】加温・加湿された水素,酸素又は空気は、
加温・加湿部51で再度各々一端に集められ、燃料電池本
体部52に戻される。燃料電池本体部52へ戻された水素,
酸素又は空気は、電極接合体53を挟み、互いに直交に流
され、電池反応が起る。反応を終え、加湿,生成水分を
含む残った水素,酸素又は空気は、各々第4セパレータ
54のF面で導入された穴の近傍から排出される。
The heated / humidified hydrogen, oxygen or air is
It is collected again at one end by the heating / humidifying section 51 and returned to the fuel cell main body section 52. Hydrogen returned to the fuel cell body 52,
Oxygen or air is flown in a direction orthogonal to each other with the electrode assembly 53 sandwiched therebetween, and a battery reaction occurs. After the reaction, the remaining hydrogen, oxygen, or air including the humidified and generated water is respectively separated by the fourth separator.
It is discharged from the vicinity of the hole introduced on the F side of 54.

【0039】なお、加温・加湿し終わり、残った冷却水
(温水)は加温・加湿部51で一端に集められ、燃料電池
本体部52の一隅を貫通して、冷却水導入穴近傍から排出
される。
After the heating / humidification is completed, the remaining cooling water (warm water) is collected at one end by the heating / humidification section 51, penetrates one corner of the fuel cell main body section 52, and from the vicinity of the cooling water introduction hole. Is discharged.

【0040】上記実施例3によれば、第1〜第3セパレ
ータ41,42,43間に第1・第2高分子膜44,45を配置し
て積層した加温・加湿部51を、電極接合体53の両サイド
に第4・第5セパレータ54,55を配置した燃料電池本体
部52に一体に組み込ませた構成になっているため、燃料
電池本体部52を冷却し温水となった冷却水を外部に取り
出すことなく、直接内部で水素,酸素又は空気を加温・
加湿させることが可能となり、燃料電池出力、冷却水
(温水)温度、水素又は空気の加湿量をセパレータ,電
極接合体,高分子膜を積層することで、任意に調整する
設定することが可能である。また、冷却水(温水)を加
温・加湿部51へ導く配管も不要でシステム全体が非常に
コンパクトで平易である。更に、水素,酸素又は空気及
び冷却水の流路を互いにに直交するように配置できるた
め、セパレータ構造も非常に簡単である。
According to the third embodiment described above, the heating / humidifying section 51 in which the first and second polymer films 44 and 45 are arranged and laminated between the first to third separators 41, 42 and 43 is used as an electrode. Since the structure is integrated into the fuel cell main body 52 in which the fourth and fifth separators 54, 55 are arranged on both sides of the joined body 53, the fuel cell main body 52 is cooled to become hot water. Heating hydrogen, oxygen or air directly inside without extracting water to the outside
It becomes possible to humidify, and the fuel cell output, cooling water (warm water) temperature, and the amount of hydrogen or air humidified can be set arbitrarily by stacking the separator, electrode assembly, and polymer membrane. is there. Further, no piping for guiding the cooling water (warm water) to the heating / humidifying section 51 is required, and the entire system is very compact and easy. Furthermore, since the flow paths of hydrogen, oxygen or air and cooling water can be arranged orthogonal to each other, the separator structure is also very simple.

【0041】なお、上記実施例では、第1〜第3セパレ
ータ間に高分子膜を配置した場合について述べたが、こ
れに限らず、多孔質体を配置してもよい。
In the above embodiment, the case where the polymer film is arranged between the first to third separators has been described, but the present invention is not limited to this, and a porous body may be arranged.

【0042】[0042]

【発明の効果】以上詳述したようにこの発明によれば、
高分子膜又は多孔質板を利用した気体の加温・加湿シス
テムを利用することにより加温・加湿装置をコンパクト
化でき、かつ加湿量を積層数の変化により飽和蒸気圧の
範囲で任意に設定でき、更に高分子膜の採用により気体
側と冷却水側の差圧を大きくとることが可能な加温・加
湿システム装置及び燃料電池を提供できる。
As described above in detail, according to the present invention,
By using a gas heating / humidifying system that uses a polymer membrane or porous plate, the heating / humidifying device can be made compact, and the amount of humidification can be set arbitrarily within the saturated vapor pressure range by changing the number of layers. Further, it is possible to provide a heating / humidifying system device and a fuel cell capable of increasing the differential pressure between the gas side and the cooling water side by adopting a polymer membrane.

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

【図1】固体高分子電解質燃料電池の発電原理を示す説
明図。
FIG. 1 is an explanatory diagram showing a power generation principle of a solid polymer electrolyte fuel cell.

【図2】従来の燃料電池の加温・加湿システム装置の説
明図。
FIG. 2 is an explanatory diagram of a conventional heating / humidifying system device for a fuel cell.

【図3】高分子膜を用いた燃料電池の加温・加湿システ
ム装置の原理を示す説明図。
FIG. 3 is an explanatory diagram showing the principle of a heating / humidifying system device for a fuel cell using a polymer membrane.

【図4】高分子膜を用いた燃料電池の燃料電池の加温・
加湿システム装置の説明図であり、図4(A)は上面
図、図4(B)は図4(A)の側面図。
[Fig. 4] Heating of a fuel cell using a polymer membrane
It is an explanatory view of a humidification system device, Drawing 4 (A) is a top view and Drawing 4 (B) is a side view of Drawing 4 (A).

【図5】多孔質板を用いた燃料電池の加温・加湿システ
ム装置の原理を示す説明図。
FIG. 5 is an explanatory diagram showing the principle of a heating / humidifying system device for a fuel cell using a porous plate.

【図6】多孔質板を用いた燃料電池の燃料電池の加温・
加湿システム装置の説明図であり、図6(A)は上面
図、図6(B)は図6(A)の側面図。
[Fig. 6] Heating of a fuel cell using a porous plate
It is explanatory drawing of a humidification system apparatus, FIG.6 (A) is a top view, FIG.6 (B) is a side view of FIG.6 (A).

【図7】溝付き多孔質板を用いた燃料電池の燃料電池の
加温・加湿システム装置の説明図であり、図7(A)は
上面図、図7(B)は図7(A)の側面図。
7A and 7B are explanatory views of a heating / humidifying system device for a fuel cell of a fuel cell using a grooved porous plate, FIG. 7A being a top view and FIG. 7B being FIG. 7A. Side view of.

【図8】本発明の実施例1に係る燃料電池の加温・加湿
システム装置の説明図。
FIG. 8 is an explanatory diagram of a heating / humidifying system device for a fuel cell according to the first embodiment of the present invention.

【図9】本発明の実施例3に係る燃料電池の説明図。FIG. 9 is an explanatory diagram of a fuel cell according to a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

41,42,43,54,55…セパレータ、 44,45…高分子
膜、46,56…水素流路、 47,58…冷
却水流路、48,57…酸素又は空気流路。
41, 42, 43, 54, 55 ... Separator, 44, 45 ... Polymer membrane, 46, 56 ... Hydrogen flow channel, 47, 58 ... Cooling water flow channel, 48, 57 ... Oxygen or air flow channel.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 高分子膜又は水を透過できる多孔質体の
両面に、加温・加湿させる気体、及び温水となった冷却
水を夫々導き、前記温水を高分子膜又は多孔質体に吸水
させ、その吸水した水を他方の面の加温・加湿させる気
体中に蒸発させるか、あるいは温水の持つ熱により同時
に加湿させることを特徴とする加温・加湿システム装
置。
1. A polymer membrane or a porous body permeable to water is introduced into both sides of a gas to be heated / humidified and cooling water which has become warm water, and the warm water is absorbed by the polymer membrane or the porous body. A heating / humidifying system device characterized by allowing the absorbed water to evaporate into a gas for heating / humidifying on the other surface, or simultaneously humidifying by the heat of the hot water.
【請求項2】 高分子膜又は水を透過できる多孔質体
と、前記高分子膜又は多孔質体の両側に配置されたセパ
レータと、前記高分子膜又は多孔質体の一方側の面に設
けられた冷却水流路と、前記高分子膜又は多孔質体の他
方側の面に設けられた加温・加湿気体流路とを具備し、
記加温・加湿させる気体を前記加湿気体流路に、また温
水となった冷却水を前記冷却水流路に夫々導き、前記温
水を高分子膜又は多孔質体に吸水させ、その吸水した水
を他方の面の加温・加湿させる気体中に蒸発させるか、
あるいは温水の持つ熱により同時に加湿させる請求項1
記載の加温・加湿システム装置。
2. A polymer membrane or a porous body permeable to water, separators arranged on both sides of the polymer membrane or the porous body, and provided on one surface of the polymer membrane or the porous body. A cooling water channel, and a heating / humidifying body channel provided on the other surface of the polymer membrane or the porous body,
The gas to be heated / humidified is introduced into the humidifying body channel, and the cooling water that has become hot water is introduced into the cooling water channel, respectively, and the warm water is absorbed by the polymer membrane or the porous body, and the absorbed water is collected. Evaporate in the gas to be heated / humidified on the other side,
Alternatively, the heat of hot water is used to simultaneously humidify.
The heating / humidification system device described.
【請求項3】 固体高分子電解質の両側に電極を夫々配
置した電極接合体と該電極接合体の両側に配置したセパ
レータとを有する燃料電池本体に、請求項2記載の加温
・加湿システム装置を一体に積層したことを特徴とする
燃料電池。
3. The heating / humidifying system device according to claim 2, wherein the fuel cell body has an electrode assembly having electrodes arranged on both sides of the solid polymer electrolyte and separators arranged on both sides of the electrode assembly. A fuel cell characterized by being integrally laminated.
JP4271855A 1992-10-09 1992-10-09 Heating and humidifying device and fuel cell Pending JPH06124722A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4271855A JPH06124722A (en) 1992-10-09 1992-10-09 Heating and humidifying device and fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4271855A JPH06124722A (en) 1992-10-09 1992-10-09 Heating and humidifying device and fuel cell

Publications (1)

Publication Number Publication Date
JPH06124722A true JPH06124722A (en) 1994-05-06

Family

ID=17505825

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4271855A Pending JPH06124722A (en) 1992-10-09 1992-10-09 Heating and humidifying device and fuel cell

Country Status (1)

Country Link
JP (1) JPH06124722A (en)

Cited By (12)

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Publication number Priority date Publication date Assignee Title
WO2000014819A1 (en) * 1998-09-04 2000-03-16 Kabushiki Kaisha Toshiba Solid polymer type fuel cell system
WO2000041261A2 (en) * 1999-01-05 2000-07-13 Siemens Aktiengesellschaft Liquid-cooled fuel cell battery comprising an integrated heat exchanger
EP1099269A4 (en) * 1998-06-03 2001-09-26 Int Fuel Cells Corp Direct mass and heat transfer fuel cell power plant
EP1298750A1 (en) * 2001-09-27 2003-04-02 Siemens Aktiengesellschaft Fuel cell battery with humidification cells
JP2005085753A (en) * 2003-09-05 2005-03-31 Asia Pacific Fuel Cell Technology Ltd Reactant gas temperature/humidity control device of fuel cell set
JP2005226945A (en) * 2004-02-13 2005-08-25 Mitsubishi Electric Corp Temperature-humidity exchanger
JP2006210149A (en) * 2005-01-28 2006-08-10 Matsushita Electric Ind Co Ltd Fuel cell system
JP2007123177A (en) * 2005-10-31 2007-05-17 Honda Motor Co Ltd Humidifier for reaction gas
US7258329B2 (en) 2004-06-15 2007-08-21 Honda Motor Co., Ltd. Reactant gas humidification apparatus and reactant gas humidification method
JP2008117686A (en) * 2006-11-07 2008-05-22 Matsushita Electric Ind Co Ltd Fuel cell system
US7745032B2 (en) 2002-10-18 2010-06-29 Hitachi, Ltd. Fuel cell with humidifier
US8129062B2 (en) 2002-04-15 2012-03-06 Panasonic Corporation Fuel cell system operation method

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1099269A4 (en) * 1998-06-03 2001-09-26 Int Fuel Cells Corp Direct mass and heat transfer fuel cell power plant
US6613467B1 (en) 1998-09-04 2003-09-02 Kabushiki Kaisha Toshiba Polymer electrolyte fuel cells system
WO2000014819A1 (en) * 1998-09-04 2000-03-16 Kabushiki Kaisha Toshiba Solid polymer type fuel cell system
WO2000041261A2 (en) * 1999-01-05 2000-07-13 Siemens Aktiengesellschaft Liquid-cooled fuel cell battery comprising an integrated heat exchanger
WO2000041261A3 (en) * 1999-01-05 2001-10-25 Siemens Ag Liquid-cooled fuel cell battery comprising an integrated heat exchanger
US7314676B2 (en) 2001-09-27 2008-01-01 Siemens Aktiengesellschaft Fuel-cell stack
EP1298750A1 (en) * 2001-09-27 2003-04-02 Siemens Aktiengesellschaft Fuel cell battery with humidification cells
WO2003030287A2 (en) * 2001-09-27 2003-04-10 Siemens Aktiengesellschaft Fuel-cell stack
WO2003030287A3 (en) * 2001-09-27 2003-10-23 Siemens Ag Fuel-cell stack
US8129062B2 (en) 2002-04-15 2012-03-06 Panasonic Corporation Fuel cell system operation method
US7745032B2 (en) 2002-10-18 2010-06-29 Hitachi, Ltd. Fuel cell with humidifier
JP2005085753A (en) * 2003-09-05 2005-03-31 Asia Pacific Fuel Cell Technology Ltd Reactant gas temperature/humidity control device of fuel cell set
JP2005226945A (en) * 2004-02-13 2005-08-25 Mitsubishi Electric Corp Temperature-humidity exchanger
US7258329B2 (en) 2004-06-15 2007-08-21 Honda Motor Co., Ltd. Reactant gas humidification apparatus and reactant gas humidification method
JP2006210149A (en) * 2005-01-28 2006-08-10 Matsushita Electric Ind Co Ltd Fuel cell system
JP2007123177A (en) * 2005-10-31 2007-05-17 Honda Motor Co Ltd Humidifier for reaction gas
JP2008117686A (en) * 2006-11-07 2008-05-22 Matsushita Electric Ind Co Ltd Fuel cell system

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