JPH10270065A - Solid polymer electrolyte fuel cell, cell unit and fuel supply method - Google Patents
Solid polymer electrolyte fuel cell, cell unit and fuel supply methodInfo
- Publication number
- JPH10270065A JPH10270065A JP9073532A JP7353297A JPH10270065A JP H10270065 A JPH10270065 A JP H10270065A JP 9073532 A JP9073532 A JP 9073532A JP 7353297 A JP7353297 A JP 7353297A JP H10270065 A JPH10270065 A JP H10270065A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- chamber
- circulating water
- cell
- oxidant
- 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.)
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Classifications
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- 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
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- Fuel Cell (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、固体高分子電解質型燃
料電池とセルユニットの改良及び燃料の供給方法に関す
るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid polymer electrolyte fuel cell, an improved cell unit, and a fuel supply method.
【0002】[0002]
【従来技術】固体高分子電解質型燃料電池は、図2、図
3に示す如く、イオン導電性であって、プロトンを移動
させる固体高分子電解質膜(21)の一方の表面にアノード
(22)、他方の表面にカソード(23)を有するセル(2)に対
し、アノード側には、燃料室(31)を有する燃料プレート
(3)、カソード側には、酸化剤室(41)を有する酸化剤プ
レート(4)を配置し、セル(2)の前後を燃料プレート(3)
と酸化剤プレート(4)とによって、サンドイッチ状に挟
んでいる。燃料プレート及び酸化剤プレートの裏面に
は、循環水の流通する循環水室(35)(45)を形成してお
り、これら3枚(2)(3)(4)から成る組を10乃至20組
束ねてユニット化したものである。燃料電池ユニットの
各燃料室(31)には、メタンガス、都市ガス等を改質して
形成した水素リッチの燃料を供給し、酸化剤室(41)に
は、酸化剤として、例えば空気を流通させる。2. Description of the Related Art As shown in FIGS. 2 and 3, a solid polymer electrolyte fuel cell is ion-conductive and has an anode on one surface of a solid polymer electrolyte membrane (21) for transferring protons.
(22) A fuel plate having a fuel chamber (31) on the anode side with respect to a cell (2) having a cathode (23) on the other surface.
(3) On the cathode side, an oxidant plate (4) having an oxidant chamber (41) is arranged, and a fuel plate (3) is provided before and after the cell (2).
And an oxidant plate (4) sandwiching the same. A circulating water chamber (35) (45) through which circulating water flows is formed on the back surface of the fuel plate and the oxidant plate, and a set of these three (2) (3) (4) They are bundled and unitized. A hydrogen-rich fuel formed by reforming methane gas, city gas, etc. is supplied to each fuel chamber (31) of the fuel cell unit, and, for example, air is circulated as an oxidant to the oxidant chamber (41). Let it.
【0003】セル(2)のアノード(22)においては、系外
より供給された水素が、At the anode (22) of the cell (2), hydrogen supplied from outside the system is
【数1】 の反応により、プロトンと電子を生成する。カソード(2
3)においては、系外から供給された酸化剤としての酸素
と、固体高分子電解質膜(21)を通って移動したプロトン
と、外部回路から流入した電子が(Equation 1) Produces protons and electrons. Cathode (2
In (3), oxygen supplied from outside the system as an oxidizing agent, protons moved through the solid polymer electrolyte membrane (21), and electrons flowing from an external circuit are generated.
【数2】 の反応により、水を生成する。(Equation 2) The reaction produces water.
【0004】[0004]
【解決すべき問題点】固体高分子電解質型燃料電池は、
容量と用途によって、一日から一週間に数回の頻度で、
停止と起動運転が行なわれる。起動の際、燃料室に何等
かの原因で空気が混入していると、燃料である水素と急
激な反応を起こして危険であるため、起動に際しては、
予め燃料室を不活性ガスによって充満し、燃料室中の残
留ガスを排除するパージが行なわれる。しかる後、燃料
ガスを供給して、通常運転が行なわれるのである。その
ため、固体高分子電解質型燃料電池においては、パージ
用の不活性ガスボンベを設置せねばならず、設備が大型
化する問題があった。[Problems to be solved] Solid polymer electrolyte fuel cells
Depending on the capacity and application, it can be performed several times a day or several times a week,
Stop and start operations are performed. At the time of startup, if air is mixed into the fuel chamber for some reason, it will cause a rapid reaction with hydrogen as fuel, and it is dangerous.
The fuel chamber is previously filled with an inert gas, and a purge is performed to remove residual gas in the fuel chamber. Thereafter, the fuel gas is supplied and normal operation is performed. Therefore, in the solid polymer electrolyte fuel cell, an inert gas cylinder for purging must be installed, and there is a problem that the equipment becomes large.
【0005】さらに、セルプレートにおける電気化学的
反応速度は、温度に依存するから、運転状態が速やかに
定常状態へ移行するには、セルを反応に適した温度、例
えば80乃至100℃に予熱する必要がある。従来は、
循環水を80℃程度の温水にして運転し、セルの循環水
室を流通させ予熱していたが、循環水室(35)(45)は、セ
ル(2)とは隔離されて、燃料プレート(3)、酸化剤プレー
ト(4)を介する間接的な加熱であるから、効率が低い問
題があった。Further, since the electrochemical reaction rate in the cell plate depends on the temperature, the cell is preheated to a temperature suitable for the reaction, for example, 80 to 100.degree. There is a need. conventionally,
The circulating water was operated with warm water of about 80 ° C, and the circulating water chamber of the cell was circulated and preheated, but the circulating water chambers (35) and (45) were isolated from the cell (2), and the fuel plate (3) Since the heating is indirect through the oxidant plate (4), the efficiency is low.
【0006】本発明は、燃料電池の起動時は、循環水通
路が燃料室を通るように切り替えることにより、循環水
によって燃料室をパージすると共に、セルを運転温度に
予熱するものである。According to the present invention, when the fuel cell is started, the fuel chamber is purged with the circulating water and the cell is preheated to the operating temperature by switching the circulating water passage so as to pass through the fuel chamber.
【0007】[0007]
【構成】本発明は、燃料室(31)及び循環水室(35)(45)の
流出側を連通し、排出弁(65)を介して循環水装置(6)に
接続し、燃料室(31)の流入側は、バイパス弁(54)及び燃
料供給弁(57)を介して燃料源へ接続すると共に、リター
ン弁(56)を介して循環水装置(6)に接続して成るもので
ある。セルユニットを構成する燃料プレートは、セル
(2)のアノード側には、燃料室(31)、他方の表面には、
循環水室(35)を有しており、酸化剤プレート(4)は、セ
ルのカソード側には、酸化剤室(41)、他の表面には、循
環水室(45)を形成しており、それぞれの循環水室(35)(4
5)は、共通の連通排出口(14)へ連通して成るものであ
る。In the present invention, the fuel chamber (31) and the outlet side of the circulating water chamber (35) (45) communicate with each other, and are connected to the circulating water device (6) via a discharge valve (65) to provide the fuel chamber ( The inlet side of (31) is connected to a fuel source via a bypass valve (54) and a fuel supply valve (57), and is connected to a circulating water device (6) via a return valve (56). is there. The fuel plate that constitutes the cell unit
On the anode side of (2), the fuel chamber (31), on the other surface,
The oxidizing plate (4) has a circulating water chamber (35) on the cathode side of the cell and a circulating water chamber (45) on the other surface. And each circulating water chamber (35) (4
5) is formed by communicating with a common communication outlet (14).
【0008】[0008]
【作用】燃料電池の起動時は、循環水装置(6)の排出弁
(65)及び燃料供給装置(5)のバイパス弁(54)を閉じると
共に、リターン弁(56)を開く。燃料及び酸化剤の送入前
に、循環水装置(6)によって、循環水を循環水室(35)(4
5)へ送入し、循環水室(35)(45)を充満させる。循環水流
出管(64)上の排出弁(65)は閉じられているから、循環水
は燃料室(31)へ流入し、燃料室をパージする。燃料室か
ら溢流した循環水は、燃料供給装置を逆流するが、燃料
供給弁(57)及びバイパス弁(54)が閉じられているから、
リターン弁(56)を経て、循環水装置(6)へ戻り、上記循
環を繰り返すのである。[Function] When the fuel cell is started, the discharge valve of the circulating water device (6)
(65) and the bypass valve (54) of the fuel supply device (5) are closed, and the return valve (56) is opened. Before feeding the fuel and the oxidizer, the circulating water is supplied to the circulating water chamber (35) (4) by the circulating water device (6).
5) to fill the circulating water chambers (35) and (45). Since the discharge valve (65) on the circulating water outflow pipe (64) is closed, the circulating water flows into the fuel chamber (31) and purges the fuel chamber. The circulating water overflowing from the fuel chamber flows back through the fuel supply device, but since the fuel supply valve (57) and the bypass valve (54) are closed,
After returning to the circulating water device (6) via the return valve (56), the above-mentioned circulation is repeated.
【0009】セルが、循環水によってパージを終了し、
且つ運転可能温度に予熱されると、排出弁(65)は開き、
燃料加湿器(52)においては、燃料供給弁(57)が開き、リ
ターン弁(56)は閉じる。従って、循環水室(35)(45)を通
過した循環水は、連通排出口(14)において合流し、排出
弁(65)、循環水流出管(64)を経て、循環水装置に戻る。
また、燃料加湿器においては、燃料供給弁(57)を経て、
燃料が各燃料室(31)へ直接供給され、燃料室を充満して
いた循環水を押し下げて、燃料室(31)には、燃料ガスが
充満し、通常運転が開始する。The cell has finished purging with circulating water,
And when preheated to the operable temperature, the discharge valve (65) opens,
In the fuel humidifier (52), the fuel supply valve (57) opens, and the return valve (56) closes. Accordingly, the circulating water that has passed through the circulating water chambers (35) and (45) merges at the communication discharge port (14), and returns to the circulating water device via the discharge valve (65) and the circulating water outflow pipe (64).
In the fuel humidifier, the fuel supply valve (57)
Fuel is directly supplied to each fuel chamber (31), and the circulating water that has filled the fuel chamber is pushed down. The fuel chamber (31) is filled with fuel gas, and normal operation starts.
【0010】[0010]
【効果】燃料電池の起動に際して、循環水を利用し、燃
料室をパージするから、燃料供給装置及び循環水装置の
弁を切り替えるだけでよく、従来の如く、パージのため
特別な不活性ガスボンベを設置する必要はない。また、
燃料室に循環水を流入して、セルを直接に加熱するか
ら、高い予熱効率が得られる。When the fuel cell is started, circulating water is used to purge the fuel chamber. Therefore, it is only necessary to switch the valves of the fuel supply device and the circulating water device. As in the conventional case, a special inert gas cylinder is used for purging. No need to install. Also,
Since the circulating water flows into the fuel chamber to directly heat the cell, high preheating efficiency can be obtained.
【0011】[0011]
【実施形態】図面及び以下の説明は、本発明の実施形態
の一つを説明するものであるから、特許請求の範囲を限
定するように解釈するために用いてはならない。燃料電
池(1)は、セル(2)と燃料プレート(3)と酸化剤プレート
(4)から成る組を10乃至20組束ねたセルユニットか
ら成っている。該セルユニットは、図2及び図3に示す
如く、各(2)(3)(4)の上部の同一位置に燃料供給口(1
1)、循環水供給口(12)、酸化剤供給口(14)を貫通、開設
している。また、各(2)(3)(4)の下部の同一位置に、横
長の連通排出口(14)及び酸化剤排出口(15)を、貫通開設
している。セル(2)を燃料プレート(3)及び酸化剤プレー
ト(4)によって、挟んだ組を複数束ねたとき、同一方向
に向う面、例えば右側に向く面をA面、左側に向く面を
B面とすると、前記した各供給口(11)(12)(13)及び排出
口(14)(15)は、同一線上に一致する。燃料プレート(3)
がセルのアノード(22)に接する面(B面)には、プレー
ト厚さの半分よりやや浅い燃料室(31)が中央に凹設さ
れ、該燃料室(31)は、燃料流入路(33)によって燃料供給
口(11)と連通し、また、燃料流出路(34)によって連通排
出口(14)に連通している。燃料室(31)の底面には、燃料
室の上辺及び下辺から離れた位置に複数本の縦リブ(32)
を並設している。燃料プレート(3)の裏面(A面)に
は、中央に循環水室(35)を凹設し、これは、循環水流入
路(37)を介して、循環水供給口(12)に連通し、循環水室
(35)の下部は、循環流出路(38)を経て、連通排出口(14)
へ通じている。BRIEF DESCRIPTION OF THE DRAWINGS The drawings and description which follow illustrate one embodiment of the present invention and should not be used to limit the scope of the claims. Fuel cell (1) consists of cell (2), fuel plate (3) and oxidizer plate
It comprises a cell unit in which 10 to 20 sets of (4) are bundled. As shown in FIGS. 2 and 3, the cell unit has a fuel supply port (1) at the same position above (2), (3) and (4).
1), circulating water supply port (12) and oxidant supply port (14). At the same position under each of (2), (3) and (4), a horizontally long communication discharge port (14) and an oxidizing agent discharge port (15) are opened. When a plurality of sets sandwiching the cell (2) by the fuel plate (3) and the oxidant plate (4) are bundled, a surface facing the same direction, for example, a surface facing the right side is a surface A, and a surface facing the left side is a surface B. Then, the supply ports (11), (12), (13) and the discharge ports (14), (15) coincide with each other on the same line. Fuel plate (3)
A fuel chamber (31), which is slightly shallower than half of the plate thickness, is recessed in the center on the surface (surface B) that contacts the anode (22) of the cell, and the fuel chamber (31) is provided with a fuel inflow passage (33). ) Communicates with the fuel supply port (11), and communicates with the communication discharge port (14) through the fuel outflow path (34). On the bottom of the fuel chamber (31), a plurality of vertical ribs (32) are located at positions away from the upper and lower sides of the fuel chamber.
Are juxtaposed. A circulating water chamber (35) is formed in the center of the back surface (A surface) of the fuel plate (3) and communicates with the circulating water supply port (12) through a circulating water inflow passage (37). And a circulating water chamber
The lower part of (35) passes through the circulation outflow channel (38) and the communication outlet (14).
Leading to
【0012】酸化剤プレート(4)がセル(2)に接する側
(A面)には、縦リブ(42)を有する酸化剤室(41)が凹設
され、該酸化剤室(41)の上部は、酸化剤供給路(43)を経
て、酸化剤供給口(13)に連通し、下部は、酸化剤排出路
(44)を経て、酸化剤排出口(15)へ連通している。酸化剤
プレート(4)の裏面(B面)は、燃料プレート(3)の裏面
(A面)と同一形状のリブ(46)付循環水室(45)及び酸化
剤の流入路(47)、流出路(48)を有している。An oxidizing agent chamber (41) having a vertical rib (42) is recessed on the side (surface A) of the oxidizing agent plate (4) in contact with the cell (2). The upper part communicates with the oxidant supply port (13) through the oxidant supply path (43), and the lower part is the oxidant discharge path.
Through (44), it communicates with the oxidant outlet (15). The back surface (surface B) of the oxidant plate (4) has the same shape as the back surface (surface A) of the fuel plate (3) with a circulating water chamber (45) with a rib (46) and an inflow passage (47) for oxidant, It has an outflow channel (48).
【0013】上記各(2)(3)(4)は、必要な数の組を向き
を揃え、密接して締め付けることにより、各燃料室(31)
は、共通の燃料供給口(11)及び連通排出口(15)へ連通す
る。また、酸化剤室(41)は、共通の供給口(13)及び排出
口(15)へ連通する。循環水室(35)(45)は、共通の供給口
(12)及び排出口(14)へ連通する。Each of the above-mentioned (2), (3) and (4) is formed by aligning the required number of sets in the same direction and tightly tightening them so that each fuel chamber (31)
Communicates with the common fuel supply port (11) and the communication discharge port (15). The oxidant chamber (41) communicates with a common supply port (13) and discharge port (15). Circulating water chambers (35) and (45) have a common supply port
(12) and the outlet (14).
【0014】図2は、セルユニットを縦断面したもので
あるが、説明の都合上、燃料供給口(14)と循環口(14)と
循環水(12)は、上下に位置をずらして描いている。酸化
剤供給口及び酸化剤排出口は、省略している。FIG. 2 is a longitudinal sectional view of the cell unit. For convenience of explanation, the fuel supply port (14), the circulation port (14), and the circulating water (12) are drawn with their positions shifted up and down. ing. The oxidant supply port and the oxidant discharge port are omitted.
【0015】燃料電池(1)は、燃料ポート(16)、循環水
ポート(17)、酸化剤ポート(18)、連通排出ポート(19)を
具え、それぞれセルユニットの燃料供給口(11)、循環水
供給口(12)、酸化剤供給口(13)、連通排出口(14)に接続
されている。循環水装置(6)は、循環水供給管(6)を水タ
ンク(66)の流出口からポンプ(62)、熱交換器(63)を経
て、循環水ポート(17)を接続し、また、排出弁(65)を有
する流出管(64)によって連通排出ポート(19)と水タンク
(66)の上部とを接続している。The fuel cell (1) includes a fuel port (16), a circulating water port (17), an oxidizer port (18), and a communication discharge port (19). The circulating water supply port (12), the oxidant supply port (13), and the communication discharge port (14) are connected. The circulating water device (6) connects the circulating water supply pipe (6) from the outlet of the water tank (66) to the circulating water port (17) via the pump (62) and the heat exchanger (63), and , A discharge tank (64) having a discharge valve (65) and a water tank communicating with a discharge port (19)
(66) is connected to the upper part.
【0016】燃料加湿器(5)は、燃料供給装置から送ら
れて来る水素リッチの燃料ガスを燃料加湿器(52)の水中
に流出させ、燃料ガスの湿度を高めて、流出口を燃料供
給管(51)によって、燃料電池(1)の燃料ポート(16)に接
続している。該燃料供給管(51)と加湿器(52)との間を、
バイパス弁(54)を有するバイパス管(53)によって接続す
ると共に、加湿器(52)の底部を、リターン弁(56)を有す
る戻し管(55)によって循環水装置(6)の水タンク(66)に
接続している。循環水は、熱交換器(63)によって約80
℃に維持されており、燃料電池(1)のセルユニットを適
温に維持するものである。The fuel humidifier (5) discharges the hydrogen-rich fuel gas sent from the fuel supply device into the water of the fuel humidifier (52), raises the humidity of the fuel gas, and supplies the fuel to the outlet. The pipe (51) is connected to the fuel port (16) of the fuel cell (1). Between the fuel supply pipe (51) and the humidifier (52),
A tub is connected by a bypass pipe (53) having a bypass valve (54), and the bottom of the humidifier (52) is connected to a water tank (66) of the circulating water device (6) by a return pipe (55) having a return valve (56). ). The circulating water is reduced to about 80 by the heat exchanger (63).
The temperature is maintained at ℃, and the cell unit of the fuel cell (1) is maintained at an appropriate temperature.
【0017】燃料電池の起動に際しては、燃料ガス及び
酸化剤の供給に先立ち、まず排出弁(65)、燃料供給弁(5
7)、バイパス弁(54)を閉じ、リターン弁(56)を開く。循
環水装置(6)の循環水経路は、排出弁(65)で止められて
いるから、循環水は、排出管(65)には流出しないが、共
通の排出口(14)を介して各燃料室(31)、燃料供給管(5
1)、加湿器(52)、リターン管(55)を経て水タンク(66)に
戻る循環路を形成する。従って、循環水室(34)(45)を通
過した循環水は、燃料水室(31)に流入し、残留ガスを押
し上げて、燃料供給管(51)を逆流し、水タンク(66)に戻
る循環が行なわれる。燃料室(31)は、セル(2)と直接接
しているから、循環水によるセル(2)の予熱は効率良く
行なわれる。When starting up the fuel cell, first, before supplying the fuel gas and the oxidizing agent, first, the discharge valve (65) and the fuel supply valve (5) are supplied.
7) Close the bypass valve (54) and open the return valve (56). Since the circulating water path of the circulating water device (6) is stopped by the discharge valve (65), the circulating water does not flow out to the discharge pipe (65), but each of the circulating water flows through the common discharge port (14). Fuel chamber (31), fuel supply pipe (5
1) Form a circulation path returning to the water tank (66) via the humidifier (52) and the return pipe (55). Therefore, the circulating water that has passed through the circulating water chambers (34) and (45) flows into the fuel water chamber (31), pushes up residual gas, flows back through the fuel supply pipe (51), and flows into the water tank (66). A return cycle is performed. Since the fuel chamber (31) is in direct contact with the cell (2), the preheating of the cell (2) by the circulating water is performed efficiently.
【0018】セル(2)が適温に達したとき、上記4つの
バルブは、手動操作又は自動的に切り替えられ、循環水
装置は、リターン管(55)を含む通路は、閉ざされ、替り
に、排出管(64)を含む通路が形成され、循環水は、循環
水室(35)(45)を充満した後、連通排出口(14)から流出管
(64)を経て、水タンク(66)へ戻る。燃料供給装置(5)
は、燃料供給弁(57)が開き、燃料は、燃料供給管(51)を
経て、燃料室(31)中の循環水を押し下げ、連通排出口(1
4)において、循環水と混合し、流出管(64)から水タンク
(66)へ流入する。水タンク(66)に戻った循環水は、再び
ポンプ(62)によって、循環水供給管(61)に送られる。水
タンク(66)で分離された未反応の残留燃料ガスは、改質
装置における燃焼ガスとして用いられる。When the temperature of the cell (2) reaches a suitable temperature, the four valves are switched manually or automatically, and the circulating water device closes the passage including the return pipe (55). A passage including the discharge pipe (64) is formed, and the circulating water fills the circulating water chamber (35) (45), and then flows out of the communication discharge port (14).
After (64), return to the water tank (66). Fuel supply device (5)
The fuel supply valve (57) is opened, and the fuel pushes down the circulating water in the fuel chamber (31) through the fuel supply pipe (51), and the communication discharge port (1
In 4), it is mixed with circulating water,
(66). The circulating water returned to the water tank (66) is sent to the circulating water supply pipe (61) again by the pump (62). The unreacted residual fuel gas separated in the water tank (66) is used as combustion gas in the reformer.
【0019】[0019]
【他の実施例】酸化剤プレート(4)の酸化剤室(41)を循
環水室(45)と連通することにより、燃料電池の起動時、
循環水室(45)から酸化剤室(41)へ循環水を流入させて、
酸化剤室(41)を直接加熱しても良い。起動時に燃料室(3
1)をパージした循環水は、必ずしもリターン管(55)、リ
ターン弁(56)を経て循環水装置(6)へ戻す必要はなく、
熱交換機(63)の容量が大きければ、外部から水を補給し
てもよい。本発明は、上記実施例に限定するものではな
く、当業者であれば、図面及び上記説明に基づき、多く
の変形を成し得ることは当然である。[Other embodiments] By connecting the oxidizing agent chamber (41) of the oxidizing agent plate (4) with the circulating water chamber (45), the fuel cell can
The circulating water flows from the circulating water chamber (45) to the oxidizing chamber (41),
The oxidant chamber (41) may be directly heated. Start the fuel chamber (3
The circulating water purged from 1) does not necessarily need to be returned to the circulating water device (6) via the return pipe (55) and the return valve (56).
If the capacity of the heat exchanger (63) is large, water may be supplied from the outside. The present invention is not limited to the above embodiments, and it is obvious that those skilled in the art can make many modifications based on the drawings and the above description.
【図1】燃料電池(1)、燃料加湿装置(5)、循環水室(6)
の配置を示す全体説明図である。[Figure 1] Fuel cell (1), fuel humidifier (5), circulating water chamber (6)
FIG. 3 is an overall explanatory diagram showing the arrangement of the holograms.
【図2】セルユニットの縦断面図であって、燃料供給口
(11)の位置をずらし、酸化剤供給口を省略して示してい
る。FIG. 2 is a longitudinal sectional view of a cell unit, showing a fuel supply port;
The position of (11) is shifted, and the oxidant supply port is omitted.
【図3】セルユニットを構成するセル、燃料プレート、
酸化剤プレートを分離して示した斜面図である。FIG. 3 shows a cell constituting a cell unit, a fuel plate,
FIG. 4 is an oblique view showing the oxidant plate separately.
【図4】セル、燃料プレート、酸化剤プレートの表面及
び裏面図であって、一方向に向う側をA面、他の方向に
向う側をB面としている。FIG. 4 is a front view and a rear view of a cell, a fuel plate, and an oxidant plate, in which a side facing one direction is a surface A and a side facing the other direction is a surface B.
(1) 燃料電池 (11) 燃料供給口 (12) 循環水供給口 (13) 酸化剤供給口 (14) 連通排出口 (15) 酸化剤排出口 (2) セル (21) 固体高分子電解質膜 (22) アノード (23) カソード (3) 燃料プレート (31) 燃料室 (35) 循環水室 (4) 酸化剤プレート (41) 酸化剤室 (45) 循環水室 (5) 燃料供給装置 (51) 燃料供給管 (53) バイパス管 (54) バイパス弁 (55) リターン管 (56) リターン弁 (57) 燃料供給弁 (6) 循環水装置 (61) 循環水供給管 (64) 循環水流出管 (65) 排出弁 (1) Fuel cell (11) Fuel supply port (12) Circulating water supply port (13) Oxidant supply port (14) Communication outlet (15) Oxidizer outlet (2) Cell (21) Solid polymer electrolyte membrane (22) Anode (23) Cathode (3) Fuel plate (31) Fuel chamber (35) Circulating water chamber (4) Oxidizer plate (41) Oxidant chamber (45) Circulating water chamber (5) Fuel supply device (51) ) Fuel supply pipe (53) Bypass pipe (54) Bypass valve (55) Return pipe (56) Return valve (57) Fuel supply valve (6) Circulating water device (61) Circulating water supply pipe (64) Circulating water outlet pipe (65) Discharge valve
───────────────────────────────────────────────────── フロントページの続き (72)発明者 西尾 晃治 大阪府守口市京阪本通2丁目5番5号 三 洋電機株式会社内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Koji Nishio 2-5-5 Keihanhondori, Moriguchi-shi, Osaka Sanyo Electric Co., Ltd.
Claims (4)
アノード(22)、他方の表面にカソード(23)を形成したセ
ル(2)に対し、カソード(23)側に酸化剤の流通する酸化
剤室(41)、アノード(22)側に燃料の流通する燃料室(31)
を配置すると共に、循環水の流通する循環水室(35)(45)
をセル(2)に近接配備し、セル(2)の温度調節を行なう燃
料電池に於て、 燃料室(31)及び循環水室(35)(45)の夫々の流出側を連通
すると共に、排出弁(65)に接続し、 燃料室(31)の流入側は、燃料供給弁(57)を介して燃料源
に接続してなる固体高分子電解質型燃料電池。1. A cell (2) having an anode (22) formed on one surface of a solid polymer electrolyte membrane (21) and a cathode (23) formed on the other surface of the solid polymer electrolyte membrane (21). The oxidizing agent chamber (41) that circulates, and the fuel chamber (31) that circulates fuel to the anode (22) side
Circulating water chamber (35) (45)
In the fuel cell for adjusting the temperature of the cell (2), the fuel cell (31) and the circulating water chambers (35) and (45) communicate with the respective outflow sides, A solid polymer electrolyte fuel cell connected to a discharge valve (65), and an inflow side of the fuel chamber (31) connected to a fuel source via a fuel supply valve (57).
アノード(22)、他方の表面にカソード(23)を形成したセ
ル(2)に対し、 該セル(2)のアノード(22)側には、一方の表面に燃料室
(31)、他方の表面に循環水室(35)を有する燃料プレート
(3)を配置し、セル(2)のカソード(23)側には、一方の表
面に酸化剤室(41)、他方の表面に循環水室(45)を有する
酸化剤プレート(4)を配置し、燃料プレート(3)の燃料室
(31)及び、燃料プレート(3)と酸化剤プレート(4)の夫々
の循環水室(35)(45)は共通の連通排出口(14)へ連通して
いる固体高分子電解質型燃料電池のセルユニット。2. A cell (2) in which an anode (22) is formed on one surface of a solid polymer electrolyte membrane (21) and a cathode (23) is formed on the other surface of the solid polymer electrolyte membrane (21). ) Side, the fuel chamber on one surface
(31), a fuel plate having a circulating water chamber (35) on the other surface
On the cathode (23) side of the cell (2), an oxidant plate (4) having an oxidant chamber (41) on one surface and a circulating water chamber (45) on the other surface is disposed. Place the fuel chamber in the fuel plate (3)
(31), and the circulating water chambers (35) and (45) of the fuel plate (3) and the oxidant plate (4) communicate with the common communication outlet (14). Cell unit.
アノード(22)、他方の表面にカソード(23)を形成したセ
ルプレート(2)に対し、カソード(23)側に酸化剤の流通
する酸化剤室(41)、アノード(22)側に燃料ガスの流通す
る燃料室(31)を配置すると共に、循環水の流通する循環
水室(35)(45)をセル(2)に近接配備し、セル(2)の温度調
節を行なう燃料電池に於て、 起動時は、燃料及び酸化剤の送入前に、循環水装置(6)
によって循環水を循環水室(35)へ送入し、循環水室(35)
を通過した循環水を燃料室(31)へ流入させて、燃料室(3
1)をパージすると共に、アノード(22)を予熱し、 通常運転時は、循環水室(35)を通過した循環水を直接に
循環水装置(6)に戻すと共に、燃料及び酸化剤を送入し
て燃料室(31)中の循環水を押し出し、燃料室(31)に燃料
を流通させることを特徴とする固体高分子電解質型燃料
電池の燃料供給方法。3. A cell plate (2) having an anode (22) formed on one surface of a solid polymer electrolyte membrane (21) and a cathode (23) formed on the other surface, and an oxidizing agent placed on the cathode (23) side. The oxidizing chamber (41) through which the fuel gas flows through the anode (22) is disposed, and the circulating water chamber (35) (45) through which the circulating water flows is disposed in the cell (2). In the fuel cell that is installed close to the cell and controls the temperature of the cell (2), at the time of startup, before the fuel and oxidant are supplied, the circulating water device (6)
The circulating water is sent to the circulating water chamber (35) by the
The circulating water passing through the fuel chamber (31) flows into the fuel chamber (3).
1), the anode (22) is preheated, and during normal operation, the circulating water that has passed through the circulating water chamber (35) is directly returned to the circulating water device (6), and fuel and oxidant are sent. A fuel supply method for a solid polymer electrolyte fuel cell, characterized in that circulating water in the fuel chamber (31) is pushed out and fuel is circulated through the fuel chamber (31).
水は燃料室(31)へ流入させると共に酸化剤室(41)にも流
入させて、カソード(23)を予熱し、通常運転時は、酸化
剤は酸化剤室(41)中の循環水を押し出して、酸化剤室(4
1)に酸化剤を流通させる請求項3に規定した固体高分子
電解質型燃料電池の燃料供給方法。When starting, the circulating water that has passed through the circulating water chamber (35) flows into the fuel chamber (31) and also into the oxidant chamber (41) to preheat the cathode (23), During normal operation, the oxidant pushes out the circulating water in the oxidant chamber (41) and
4. The fuel supply method for a solid polymer electrolyte fuel cell according to claim 3, wherein the oxidant is passed through 1).
Priority Applications (1)
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JP07353297A JP3571167B2 (en) | 1997-03-26 | 1997-03-26 | Solid polymer electrolyte fuel cell, cell unit, and fuel supply method |
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Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP07353297A JP3571167B2 (en) | 1997-03-26 | 1997-03-26 | Solid polymer electrolyte fuel cell, cell unit, and fuel supply method |
Publications (2)
Publication Number | Publication Date |
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JPH10270065A true JPH10270065A (en) | 1998-10-09 |
JP3571167B2 JP3571167B2 (en) | 2004-09-29 |
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JP07353297A Expired - Fee Related JP3571167B2 (en) | 1997-03-26 | 1997-03-26 | Solid polymer electrolyte fuel cell, cell unit, and fuel supply method |
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Cited By (5)
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JP2000195534A (en) * | 1998-12-24 | 2000-07-14 | Toyota Motor Corp | Fuel cell system |
JP2000306594A (en) * | 1999-04-20 | 2000-11-02 | Toyota Motor Corp | Fuel cell system |
WO2001003215A1 (en) * | 1999-06-30 | 2001-01-11 | Ballard Power Systems Inc. | Method and apparatus for increasing the temperature of a fuel cell with polymer electrolyte |
US6472090B1 (en) | 1999-06-25 | 2002-10-29 | Ballard Power Systems Inc. | Method and apparatus for operating an electrochemical fuel cell with periodic reactant starvation |
WO2008129793A1 (en) | 2007-03-22 | 2008-10-30 | Panasonic Corporation | Method for operating fuel cell system, and fuel cell system |
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JPH0541230A (en) * | 1990-08-03 | 1993-02-19 | Fuji Electric Co Ltd | Solid high molecular electrolyte type fuel cell, and method of supplying water to be absorbed into film and gas |
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WO2008129793A1 (en) | 2007-03-22 | 2008-10-30 | Panasonic Corporation | Method for operating fuel cell system, and fuel cell system |
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Free format text: JAPANESE INTERMEDIATE CODE: R250 |
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LAPS | Cancellation because of no payment of annual fees |