JP2002367630A - Fuel cell - Google Patents

Fuel cell

Info

Publication number
JP2002367630A
JP2002367630A JP2001172467A JP2001172467A JP2002367630A JP 2002367630 A JP2002367630 A JP 2002367630A JP 2001172467 A JP2001172467 A JP 2001172467A JP 2001172467 A JP2001172467 A JP 2001172467A JP 2002367630 A JP2002367630 A JP 2002367630A
Authority
JP
Japan
Prior art keywords
flow path
gas flow
oxygen
fuel cell
hydrogen
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
Application number
JP2001172467A
Other languages
Japanese (ja)
Other versions
JP3630113B2 (en
Inventor
Mineo Wajima
峰生 和島
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.)
Hitachi Cable Ltd
Original Assignee
Hitachi Cable 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 Hitachi Cable Ltd filed Critical Hitachi Cable Ltd
Priority to JP2001172467A priority Critical patent/JP3630113B2/en
Publication of JP2002367630A publication Critical patent/JP2002367630A/en
Application granted granted Critical
Publication of JP3630113B2 publication Critical patent/JP3630113B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Abstract

PROBLEM TO BE SOLVED: To provide a fuel cell with good drainage. SOLUTION: The fuel cell is formed by interposing a solid polymer electrolyte 10 between a hydrogen supplying plate 13, having flow paths 20, 21 through which, the gas containing hydrogen and oxygen or air as main fuel flows, and an oxygen supplying plate 14, through electrodes 11, 12 having catalyst. The cross section of the gas flow path 21 of the oxygen supplying plate 14 is made bigger than the cross section of the gas flow path 20 of the hydrogen supplying plate 13.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、固体高分子電解質
膜を用いた燃料電池に関するものである。
TECHNICAL FIELD The present invention relates to a fuel cell using a solid polymer electrolyte membrane.

【0002】[0002]

【従来の技術】従来の燃料電池は、例えば、固体高分子
電解質を用いたものは、図10に示すように、固体電解
質100を挟んで、触媒101,102、水素極(負
極)103,防水膜105が設けられた空気極(正極)
104で構成されている。水素極103では外部から供
給された水素ガスが、水素極103内を通過させて反応
帯域近くに達し、触媒101に吸収されて活性な水素に
なる。
2. Description of the Related Art In a conventional fuel cell using a solid polymer electrolyte, for example, as shown in FIG. 10, a catalyst 101, 102, a hydrogen electrode (negative electrode) 103, a waterproof Air electrode (positive electrode) provided with membrane 105
104. At the hydrogen electrode 103, hydrogen gas supplied from the outside passes through the hydrogen electrode 103, reaches near the reaction zone, is absorbed by the catalyst 101, and becomes active hydrogen.

【0003】この水素原子は、次式のように電解質中の
水酸イオンと反応して水となり、その際、電子を空気極
104に送る。
[0003] The hydrogen atoms react with hydroxyl ions in the electrolyte to become water as shown in the following formula, and at this time, electrons are sent to the air electrode 104.

【0004】 H2 + 2OH- → 2H2 O + 2e- 一方、空気極104では、触媒の存在の下で、空気極1
04から2個の電子を受け取り、外部から供給された酸
素分子が、電解質100からの水と反応して、水酸イオ
ンを生成する。
H 2 + 2OH → 2H 2 O + 2e On the other hand, at the air electrode 104, the air electrode 1
Two electrons are received from the substrate 04 and oxygen molecules supplied from the outside react with water from the electrolyte 100 to generate hydroxyl ions.

【0005】1/2O2 + H2 O → 2OH- この空気極で生成した水酸イオンは、電解質100中を
移動してきた水素イオンと反応して水を生成し、全体の
回路を形成する。
[0005] 1 / 2O 2 + H 2 O → 2OH - hydroxy generated in the air electrode ions react with hydrogen ions moved to the middle electrolyte 100 to form water, to form a circuit of the whole.

【0006】従って、電池全体の反応は、 H2 + 1/2O2 → 2H2 O となり、燃料ガス中の水素と空気中の酸素が反応し水が
生成する反応となる。
Accordingly, the reaction of the whole battery is H 2 + 1 / 2O 2 → 2H 2 O, and hydrogen in the fuel gas and oxygen in the air react to generate water.

【0007】[0007]

【発明が解決しようとする課題】さて、実際の燃料電池
セルは、図11のように電解質100を、空気供給プレ
ート106と水素供給プレート107で挟んで構成さ
れ、空気供給プレート106に、酸素供給管108と排
水管109が接続され、水素供給プレート107に水素
供給管110と排ガス管(図示せず)が接続される。
As shown in FIG. 11, an actual fuel cell comprises an electrolyte 100 sandwiched between an air supply plate 106 and a hydrogen supply plate 107. A pipe 108 and a drain pipe 109 are connected, and a hydrogen supply pipe 110 and an exhaust gas pipe (not shown) are connected to the hydrogen supply plate 107.

【0008】図12は、図11のF−F線断面図を示し
たもので、空気供給プレート106と水素供給プレート
107で、電解質100を負極側触媒付き電極シート1
11と正極側触媒電極シート(防水シート付き)112
を介して挟み、水素ガスや、酸素ガスを配管し供給する
構造をとる。多くの場合、空気供給プレート106と水
素供給プレート107にガス流路113,114を形成
し、さらに電極シート111,112に溝115,11
6を設けている。
FIG. 12 is a cross-sectional view taken along line FF of FIG. 11. The air supply plate 106 and the hydrogen supply plate 107 are used to connect the electrolyte 100 to the negative electrode side electrode sheet 1 with a catalyst.
11 and positive electrode side catalyst electrode sheet (with waterproof sheet) 112
And a structure in which hydrogen gas or oxygen gas is supplied by piping. In many cases, gas passages 113 and 114 are formed in the air supply plate 106 and the hydrogen supply plate 107, and the grooves 115 and 11 are formed in the electrode sheets 111 and 112.
6 are provided.

【0009】実用上は多数の積層構造をとるため、電極
間にセパレータなどで絶縁分離している。従って、セル
を組み立てるには、ガス漏れに対する配慮を各セル周囲
全部に対して施す必要があり、またこの板状のものに配
管を設け、原料ガスを供給してやる必要がある。
In practice, in order to form a multi-layer structure, the electrodes are insulated and separated by a separator or the like. Therefore, in assembling the cells, it is necessary to give consideration to gas leakage to the entire periphery of each cell, and it is necessary to provide a pipe on this plate-shaped member and supply the raw material gas.

【0010】また、電解質のイオンの移動効率に関して
電解質の水分濃度のコントロールが重要である。
It is important to control the concentration of water in the electrolyte with respect to the ion transfer efficiency of the electrolyte.

【0011】図11,12に示すような従来の燃料電池
セルではガス流路が狭く長くなり、ガスの流れの抵抗が
大きくなったり、水分が凝縮して水滴ができ、排水がう
まくできず、酸化ガスが到達しないところや、水分濃度
分布のばらつきを生じていた。
In the conventional fuel cell shown in FIGS. 11 and 12, the gas flow path is narrow and long, the resistance of the gas flow is increased, and water is condensed to form water droplets. There were places where the oxidizing gas did not reach, and variations in the water concentration distribution occurred.

【0012】そこで、本発明の目的は、上記課題を解決
し、排水が良好に行える燃料電池を提供することにあ
る。
Accordingly, an object of the present invention is to solve the above-mentioned problems and to provide a fuel cell which can drain well.

【0013】[0013]

【課題を解決するための手段】上記目的を達成するため
に、請求項1の発明は、固体高分子電解質を、触媒付き
電極を介して水素と酸素又は空気を主燃料とするガスを
流すガス流路が形成された水素供給プレートと酸素供給
プレートで挟んで形成した燃料電池において、酸素供給
プレートのガス流路断面を水素供給プレートのガス流路
より大きく形成した燃料電池である。
In order to achieve the above object, the invention of claim 1 is directed to a method in which a solid polymer electrolyte is supplied through a catalyst-equipped electrode by flowing a gas containing hydrogen and oxygen or air as a main fuel. A fuel cell formed between a hydrogen supply plate having a flow path and an oxygen supply plate, wherein a gas flow path cross section of the oxygen supply plate is formed larger than a gas flow path of the hydrogen supply plate.

【0014】請求項2の発明は、酸素供給プレートを二
段に形成し、その酸素供給プレートにガス流路を形成し
た請求項1記載の燃料電池である。
According to a second aspect of the present invention, there is provided the fuel cell according to the first aspect, wherein the oxygen supply plate is formed in two stages, and a gas flow path is formed in the oxygen supply plate.

【0015】請求項3の発明は、筒状に形成した固体高
分子電解質の内外にそれぞれガス流路を形成する電極を
設け、その酸素供給側のガス流路断面を水素供給側より
大きく形成した燃料電池である。
According to a third aspect of the present invention, electrodes for forming gas flow paths are provided inside and outside the solid polymer electrolyte formed in a cylindrical shape, and the cross section of the gas flow path on the oxygen supply side is formed larger than the hydrogen supply side. It is a fuel cell.

【0016】請求項4の発明は、固体高分子電解質の内
周に、外周に酸素供給用のガス流路が形成された筒状の
正極側内部電極を設け、固体高分子電解質の外周に、内
周に水素供給用のガス流路が形成された筒状の負極側外
部電極を設け、上記正極側内部電極の中心に酸素供給用
のガス流路で生成した水を排水する通路を形成した請求
項3記載の燃料電池である。
According to a fourth aspect of the present invention, a cylindrical internal electrode having a cylindrical positive electrode having a gas flow path for supplying oxygen on the outer periphery is provided on the inner periphery of the solid polymer electrolyte. A cylindrical negative electrode external electrode having a hydrogen supply gas flow path formed on the inner periphery was provided, and a passage for draining water generated in the oxygen supply gas flow path was formed at the center of the positive electrode internal electrode. A fuel cell according to claim 3.

【0017】請求項5の発明は、通路に排水管が接続さ
れ、その排水管に、酸素供給用のガス流路の水分濃度を
制御する除湿器が接続された請求項4記載の燃料電池で
ある。
According to a fifth aspect of the present invention, there is provided the fuel cell according to the fourth aspect, wherein a drain pipe is connected to the passage, and a dehumidifier for controlling the moisture concentration of the gas path for supplying oxygen is connected to the drain pipe. is there.

【0018】請求項6の発明は、固体高分子電解質の内
周に、外周に水素供給用のガス流路が形成された筒状の
負極側内部電極を設け、固体高分子電解質の外周に、内
周に酸素供給用のガス流路が形成された2重の筒状体か
らなる正極側外部電極を設けた請求項3記載の燃料電池
である。
According to a sixth aspect of the present invention, there is provided a cylindrical negative electrode side inner electrode having a hydrogen supply gas flow path formed on the outer periphery on the inner periphery of the solid polymer electrolyte. 4. The fuel cell according to claim 3, wherein a positive electrode side external electrode formed of a double cylindrical body having an oxygen supply gas flow path formed on an inner periphery thereof is provided.

【0019】請求項7の発明は、正極側外部電極のガス
流路に排水管を接続し、その排水管に、酸素供給用のガ
ス流路の水分濃度を制御する除湿器が接続された請求項
6記載の燃料電池である。
According to a seventh aspect of the present invention, a drain pipe is connected to the gas flow path of the positive electrode side external electrode, and a dehumidifier for controlling the water concentration of the gas flow path for supplying oxygen is connected to the drain pipe. Item 7. A fuel cell according to Item 6.

【0020】[0020]

【発明の実施の形態】以下、本発明の好適実施の形態を
添付図面に基づいて詳述する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below in detail with reference to the accompanying drawings.

【0021】図1〜3は、本発明の燃料電池の概略図を
示したものである。
1 to 3 show schematic views of a fuel cell according to the present invention.

【0022】先ず、図1は本発明の燃料電池の概略斜視
図を示し、図2は、図1のA−A線断面図を示し、図3
は図2の断面図を斜めから見た概念図を示す。
FIG. 1 is a schematic perspective view of a fuel cell according to the present invention, FIG. 2 is a sectional view taken along line AA of FIG.
Shows a conceptual diagram of the cross-sectional view of FIG. 2 as viewed obliquely.

【0023】燃料電池セルは、固体電解質10に、負極
側触媒電極シート(防水シート付き)11と正極側電極
シート12が設けられ、更に負極側水素供給プレート1
3と正極側酸素供給プレート14とで挟まれて形成さ
れ、その水素供給プレート13と正極側酸素供給プレー
ト14間の周囲にシール剤15が設けられて構成され、
水素供給プレート13に水素供給管16が、酸素供給プ
レート14に酸素供給管17と排水管18が接続され
る。
In the fuel cell unit, a solid electrolyte 10 is provided with a negative electrode-side catalyst electrode sheet (with a waterproof sheet) 11 and a positive electrode side electrode sheet 12.
3 and a positive electrode side oxygen supply plate 14, and a sealant 15 is provided around the hydrogen supply plate 13 and the positive electrode side oxygen supply plate 14,
A hydrogen supply pipe 16 is connected to the hydrogen supply plate 13, and an oxygen supply pipe 17 and a drain pipe 18 are connected to the oxygen supply plate 14.

【0024】水素供給プレート13と酸素供給プレート
14には、電極シート11,12に水素と酸素を供給す
るためのガス流路20,21がそれぞれ形成される。
In the hydrogen supply plate 13 and the oxygen supply plate 14, gas flow paths 20, 21 for supplying hydrogen and oxygen to the electrode sheets 11, 12 are formed, respectively.

【0025】この酸素供給プレート14は、従来の酸素
供給プレートを二枚重ね、そのガス流路21が適宜箇所
で上下つながって形成される。
The oxygen supply plate 14 is formed by stacking two conventional oxygen supply plates and connecting gas passages 21 at appropriate locations in the vertical direction.

【0026】この燃料電池において、負極側水素供給プ
レート13のガス流路20に水素供給管16から水素が
供給され、酸素供給プレート14のガス流路21に酸素
供給管17から酸素又は酸素源としての空気が供給され
て反応され、電力が発生し、生成した水が、ガス流路2
1から排出される。
In this fuel cell, hydrogen is supplied from the hydrogen supply pipe 16 to the gas flow path 20 of the hydrogen supply plate 13 on the negative electrode side, and oxygen or an oxygen source is supplied from the oxygen supply pipe 17 to the gas flow path 21 of the oxygen supply plate 14. Is supplied and reacted, electric power is generated, and the generated water is supplied to the gas passage 2
Emitted from 1.

【0027】この際、ガス流路21は、その流路断面が
大きく形成されるため、排水が良好となる。
At this time, since the gas flow path 21 has a large cross section, the drainage becomes good.

【0028】また図1〜図3には示していないが、酸素
供給プレート14の酸素又は酸素源側の排水管18のポ
ートの先には、圧力調整弁、除湿器が接続されており、
セル内の水分濃度を調整する。
Although not shown in FIGS. 1 to 3, a pressure regulating valve and a dehumidifier are connected to the end of the port of the drain pipe 18 on the oxygen or oxygen source side of the oxygen supply plate 14,
Adjust the water concentration in the cell.

【0029】この燃料電池の運転は、1例として、水素
を2気圧、酸素は1気圧とした。又酸素源として空気を
用いた場合、圧力を5気圧にした。
In the operation of this fuel cell, for example, hydrogen was set at 2 atm and oxygen was set at 1 atm. When air was used as the oxygen source, the pressure was 5 atm.

【0030】このように作成した燃料電池セルに上述の
燃料ガスを供給して運転したところ、0.8Vの起電力
が発生した。
When the fuel cell described above was supplied with the above-mentioned fuel gas and operated, an electromotive force of 0.8 V was generated.

【0031】プレート13,14は、多段に積層されセ
パレータとしての機能を有し、炭素が主原料の圧縮加工
品を用いるが、通電性があり、機密性が保たれ、腐食さ
れなければ、特に材料に拠らない。
The plates 13 and 14 are stacked in multiple stages and have a function as a separator. A compression-processed product made of carbon as a main raw material is used. Not dependent on material.

【0032】図4〜図6は、本発明の他の実施の形態を
示したもので、図4は、燃料電池の概略全体図、図5
は、図4のB−B線断面図、図6は図4のC−C線断面
図を示す。
FIGS. 4 to 6 show another embodiment of the present invention. FIG. 4 is a schematic overall view of a fuel cell, and FIGS.
4 is a sectional view taken along line BB of FIG. 4, and FIG. 6 is a sectional view taken along line CC of FIG.

【0033】先ず燃料電池セル28は、円柱型に形成さ
れ、円筒状に形成した固体高分子電解質30を挟んで、
筒状の正極側内部電極32と筒状の負極側外部電極34
とが設けられて構成される。この正極側内部電極32の
外周には、固体高分子電解質30に酸素を供給すべく溝
状のガス流路31が形成され、負極側外部電極34の内
周には、固体高分子電解質30に水素を供給すべく溝状
のガス流路33が形成される。この正極側内部電極32
の中心側には、ガス流路31とつながり、酸素の供給と
生成水を排出するための通路35が形成される。なお、
触媒層、防水層は図では省略しているが設けられてい
る。
First, the fuel cell 28 is formed in a columnar shape, and sandwiches a solid polymer electrolyte 30 formed in a cylindrical shape.
A cylindrical positive electrode side internal electrode 32 and a cylindrical negative electrode side external electrode 34
Are provided. A groove-shaped gas flow path 31 is formed on the outer periphery of the positive electrode side internal electrode 32 so as to supply oxygen to the solid polymer electrolyte 30, and the inner periphery of the negative electrode side external electrode 34 is formed on the solid polymer electrolyte 30. A groove-shaped gas flow path 33 is formed to supply hydrogen. This positive electrode side internal electrode 32
A passage 35 for supplying oxygen and discharging generated water is formed on the center side of the gas passage 31. In addition,
The catalyst layer and the waterproof layer are provided although omitted in the figure.

【0034】図4に示すように、水素ガス源40には供
給配管41が接続され、その供給配管41が、負極側外
部電極34のガス流路33とつながるガス通路43に接
続され、他方、酸素ガス源44には、ガス配管45が接
続され、その配管45が通路35に接続され、その通路
35の下部に排水管46が接続され、その排水管46に
圧力調整弁と冷却器などからなる除湿器47が接続さ
れ、その除湿器47で除去された水が排水孔48より排
水されるようになっている。
As shown in FIG. 4, a supply pipe 41 is connected to the hydrogen gas source 40, and the supply pipe 41 is connected to a gas passage 43 connected to the gas flow path 33 of the negative electrode 34. A gas pipe 45 is connected to the oxygen gas source 44, the pipe 45 is connected to a passage 35, a drain pipe 46 is connected to a lower portion of the passage 35, and the drain pipe 46 is connected to a pressure regulating valve, a cooler, and the like. A dehumidifier 47 is connected, and the water removed by the dehumidifier 47 is drained from a drain hole 48.

【0035】なお、49は電流電圧計である。Reference numeral 49 denotes a current / voltmeter.

【0036】この実施の形態においては、水素ガス源4
0と酸素ガス源44からの燃料ガスの供給は、ガス流路
33,31に供給して軸方向に流すだけなので配管が容
易となる。
In this embodiment, the hydrogen gas source 4
Since the supply of the fuel gas from the O and oxygen gas sources 44 is merely performed by supplying the gas to the gas flow paths 33 and 31 and flowing in the axial direction, the piping becomes easy.

【0037】また正極側からの生成水は、ガス流路31
と通路35とがつながり流路断面が、水素のガス流路3
3より実質的に大きく形成され、ガス流路31で生成し
た水はそのガス流路31から通路35に排出され、排水
管46を通して良好に排水できる。
The water produced from the positive electrode side is supplied to the gas passage 31
And the passage 35 are connected to each other, and the cross section of the passage is the hydrogen gas passage 3
3, the water generated in the gas flow path 31 is discharged from the gas flow path 31 to the passage 35, and can be drained well through the drain pipe 46.

【0038】この際、除湿器47で、排水孔48に排水
する排水量を調整することで、ガス流路31内での水分
濃度を自在に調整できると共にそのガス流路31内で水
分が凝集して排水が不良になることもない。
At this time, by adjusting the amount of water drained to the drain hole 48 by the dehumidifier 47, the water concentration in the gas passage 31 can be freely adjusted, and the water condenses in the gas passage 31. The drainage does not become bad.

【0039】図7〜図9は、本発明の他の実施の形態を
示したもので、図7は、燃料電池の概略全体図、図8
は、図7のD−D線断面図、図9は図7のE−E線断面
図を示す。
7 to 9 show another embodiment of the present invention. FIG. 7 is a schematic overall view of a fuel cell, and FIG.
7 is a sectional view taken along line DD of FIG. 7, and FIG. 9 is a sectional view taken along line EE of FIG.

【0040】先ず燃料電池セル52は、円柱型に形成さ
れ、固体電解質50を挟んで、水素のガス流路53が形
成された負極側内部電極54と、酸素の第1ガス流路5
5が形成された正極側外部第1電極56が設けられ、そ
の外側に第2ガス流路57が形成された正極側外部第2
電極58が設けられて構成され、その第1ガス流路55
と第2ガス流路57とが適宜箇所でつながって形成され
る。なお、触媒層、防水層は図では省略しているが設け
られている。
First, the fuel cell 52 is formed in a cylindrical shape, and has a negative electrode side internal electrode 54 having a hydrogen gas flow path 53 formed therebetween with a solid electrolyte 50 interposed therebetween, and an oxygen first gas flow path 5.
5 is provided, and a positive electrode side external second electrode 56 having a second gas flow path 57 formed outside thereof is provided.
An electrode 58 is provided and the first gas flow path 55 is provided.
And the second gas flow path 57 are connected to each other at an appropriate position and formed. The catalyst layer and the waterproof layer are provided although omitted in the figure.

【0041】図7に示すように、酸素ガス源60には供
給配管61が接続され、その供給配管61が、正極側第
1外部電極56と第2外部電極58のガス流路55,5
7とつながるガス通路63に接続され、他方、水素ガス
源64には、ガス配管65が接続され、その配管65が
負極側内部電極54のガス流路53に接続される。
As shown in FIG. 7, a supply pipe 61 is connected to the oxygen gas source 60, and the supply pipe 61 is connected to the gas flow paths 55, 5 of the positive first external electrode 56 and the second external electrode 58.
A gas pipe 65 is connected to the hydrogen gas source 64, and the pipe 65 is connected to the gas channel 53 of the negative electrode 54.

【0042】また燃料電池セル52の下部の排水管66
は、第1ガス流路55と第2ガス流路57と接続され、
その排水管66に圧力調整弁と冷却器などからなる除湿
器67が接続され、その除湿器67で除去された水が排
水孔68より排水されるようになっている。
The drain pipe 66 below the fuel cell 52
Is connected to the first gas passage 55 and the second gas passage 57,
A dehumidifier 67 including a pressure regulating valve and a cooler is connected to the drain pipe 66, and water removed by the dehumidifier 67 is drained from a drain hole 68.

【0043】なお、69は電流電圧計である。Reference numeral 69 denotes an ammeter.

【0044】この実施の形態においては、図4〜6の形
態と逆に、水素ガス源64のガスを中心側に、酸素ガス
源60からの酸素を外側に流し、その酸素のガス流路5
5,57を2段にし形成して流すことで、良好に排水で
きる。この際、除湿器67で、排水孔68に排水する排
水量を調整することで、ガス流路55,57内での水分
濃度を自在に調整できると共にそのガス流路55,57
内で水分が凝集して排水が不良になることもない。
In this embodiment, contrary to the embodiments shown in FIGS. 4 to 6, the gas from the hydrogen gas source 64 is made to flow toward the center and the oxygen from the oxygen gas source 60 is made to flow to the outside.
By forming and flowing 5,57 in two stages, it is possible to drain well. At this time, by adjusting the amount of water discharged to the drain hole 68 by the dehumidifier 67, the water concentration in the gas flow paths 55 and 57 can be freely adjusted and the gas flow paths 55 and 57 can be adjusted.
There is no possibility that the water will condense in the inside and the drainage will become defective.

【0045】このように円柱型の燃料電池とすること
で、複数セルに対して各ガス流路への配管が容易とな
る。また燃料電池セルは、縦でも横でも、生成される水
の排水を考慮すればどちらでも構わない。また円柱型の
セルの太さは、原理的には起電力に依存しないので、自
由に設計できる。
By using a columnar fuel cell as described above, piping to each gas flow path for a plurality of cells becomes easy. The fuel cell may be either vertical or horizontal, taking into consideration the generated water drainage. In addition, the thickness of the cylindrical cell does not depend on the electromotive force in principle, and can be freely designed.

【0046】[0046]

【発明の効果】以上要するに本発明によれば、酸素のガ
ス流路を2段などに形成して広く形成することで、排水
を良好にすることができる。
As described above, according to the present invention, the drainage can be improved by forming the oxygen gas flow path in two steps and widening the flow path.

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

【図1】本発明の一実施の形態を示す図である。FIG. 1 is a diagram showing an embodiment of the present invention.

【図2】図1のA−A線断面図を示す。FIG. 2 is a sectional view taken along line AA of FIG.

【図3】図3は図2の断面図を斜めから見た概念図を示
す。
FIG. 3 is a conceptual diagram of the cross-sectional view of FIG. 2 as viewed obliquely.

【図4】本発明の他の実施の形態の燃料電池の概略全体
図である。
FIG. 4 is a schematic overall view of a fuel cell according to another embodiment of the present invention.

【図5】図4のB−B線断面図である。FIG. 5 is a sectional view taken along line BB of FIG. 4;

【図6】図4のC−C線断面図を示す。FIG. 6 is a sectional view taken along line CC of FIG. 4;

【図7】本発明の他の実施の形態の燃料電池の概略全体
図である。
FIG. 7 is a schematic overall view of a fuel cell according to another embodiment of the present invention.

【図8】図7のD−D線断面図である。FIG. 8 is a sectional view taken along line DD of FIG. 7;

【図9】図7のE−E線断面図である。FIG. 9 is a sectional view taken along line EE of FIG. 7;

【図10】燃料電池セルの基本構造を示す図である。FIG. 10 is a diagram showing a basic structure of a fuel cell unit.

【図11】従来の燃料電池セルを示す概略斜視図であ
る。
FIG. 11 is a schematic perspective view showing a conventional fuel cell unit.

【図12】図11のF−F線断面図である。FIG. 12 is a sectional view taken along line FF of FIG. 11;

【符号の説明】[Explanation of symbols]

10 固体高分子電解質 11,12 触媒付き電極 13 水素供給プレート 14 酸素供給プレート 20,21 ガス流路 DESCRIPTION OF SYMBOLS 10 Solid polymer electrolyte 11, 12 Electrode with a catalyst 13 Hydrogen supply plate 14 Oxygen supply plate 20, 21 Gas flow path

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 固体高分子電解質を、触媒付き電極を介
して水素と酸素又は空気を主燃料とするガスを流すガス
流路が形成された水素供給プレートと酸素供給プレート
で挟んで形成した燃料電池において、酸素供給プレート
のガス流路断面を水素供給プレートのガス流路より大き
く形成したことを特徴とする燃料電池。
1. A fuel comprising a solid polymer electrolyte sandwiched between an oxygen supply plate and a hydrogen supply plate having a gas flow path through which a gas containing hydrogen and oxygen or air as a main fuel is formed via an electrode with a catalyst. A fuel cell, wherein a cross section of a gas passage of an oxygen supply plate is formed larger than a gas passage of a hydrogen supply plate.
【請求項2】 酸素供給プレートを二段に形成し、その
酸素供給プレートにガス流路を形成した請求項1記載の
燃料電池。
2. The fuel cell according to claim 1, wherein the oxygen supply plate is formed in two stages, and a gas flow path is formed in the oxygen supply plate.
【請求項3】 筒状に形成した固体高分子電解質の内外
にそれぞれガス流路を形成する電極を設け、その酸素供
給側のガス流路断面を水素供給側より大きく形成したこ
とを特徴とする燃料電池。
3. An electrode for forming a gas flow path inside and outside a solid polymer electrolyte formed in a cylindrical shape, and a cross section of the gas flow path on the oxygen supply side is formed larger than that on the hydrogen supply side. Fuel cell.
【請求項4】 固体高分子電解質の内周に、外周に酸素
供給用のガス流路が形成された筒状の正極側内部電極を
設け、固体高分子電解質の外周に、内周に水素供給用の
ガス流路が形成された筒状の負極側外部電極を設け、上
記正極側内部電極の中心に酸素供給用のガス流路で生成
した水を排水する通路を形成した請求項3記載の燃料電
池。
4. A cylindrical positive electrode having a gas flow path for supplying oxygen on the outer periphery thereof is provided on the inner periphery of the solid polymer electrolyte, and hydrogen is supplied on the outer periphery of the solid polymer electrolyte and on the inner periphery thereof. 4. A cylindrical negative electrode-side external electrode having a gas flow path formed therein, and a passage for draining water generated in the gas flow path for oxygen supply is formed at the center of the internal electrode on the positive electrode side. Fuel cell.
【請求項5】 通路に排水管が接続され、その排水管
に、酸素供給用のガス流路の水分濃度を制御する除湿器
が接続された請求項4記載の燃料電池。
5. The fuel cell according to claim 4, wherein a drain pipe is connected to the passage, and a dehumidifier for controlling the moisture concentration in the gas flow path for supplying oxygen is connected to the drain pipe.
【請求項6】 固体高分子電解質の内周に、外周に水素
供給用のガス流路が形成された筒状の負極側内部電極を
設け、固体高分子電解質の外周に、内周に酸素供給用の
ガス流路が形成された2重の筒状体からなる正極側外部
電極を設けた請求項3記載の燃料電池。
6. A cylindrical negative electrode having a gas flow path for supplying hydrogen on the outer periphery thereof is provided on the inner periphery of the solid polymer electrolyte, and oxygen is supplied on the outer periphery of the solid polymer electrolyte and on the inner periphery thereof. The fuel cell according to claim 3, further comprising a positive electrode-side external electrode formed of a double cylindrical body having a gas flow path formed therein.
【請求項7】 正極側外部電極のガス流路に排水管を接
続し、その排水管に、酸素供給用のガス流路の水分濃度
を制御する除湿器が接続された請求項6記載の燃料電
池。
7. The fuel according to claim 6, wherein a drain pipe is connected to the gas flow path of the positive electrode side external electrode, and a dehumidifier for controlling the moisture concentration of the gas flow path for supplying oxygen is connected to the drain pipe. battery.
JP2001172467A 2001-06-07 2001-06-07 Fuel cell Expired - Fee Related JP3630113B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001172467A JP3630113B2 (en) 2001-06-07 2001-06-07 Fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001172467A JP3630113B2 (en) 2001-06-07 2001-06-07 Fuel cell

Publications (2)

Publication Number Publication Date
JP2002367630A true JP2002367630A (en) 2002-12-20
JP3630113B2 JP3630113B2 (en) 2005-03-16

Family

ID=19014083

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3630113B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006216420A (en) * 2005-02-04 2006-08-17 Toyota Motor Corp Membrane electrode composite for fuel cell
WO2007026955A2 (en) * 2005-08-31 2007-03-08 Toyota Jidosha Kabushiki Kaisha Fuel cell
JP2007087860A (en) * 2005-09-26 2007-04-05 Equos Research Co Ltd Cell and stack of fuel cell
US7838064B2 (en) 2005-08-31 2010-11-23 Toyota Jidosha Kabushiki Kaisha Method for manufacturing tube-type fuel cell

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006216420A (en) * 2005-02-04 2006-08-17 Toyota Motor Corp Membrane electrode composite for fuel cell
WO2007026955A2 (en) * 2005-08-31 2007-03-08 Toyota Jidosha Kabushiki Kaisha Fuel cell
WO2007026955A3 (en) * 2005-08-31 2008-09-18 Toyota Motor Co Ltd Fuel cell
US7838064B2 (en) 2005-08-31 2010-11-23 Toyota Jidosha Kabushiki Kaisha Method for manufacturing tube-type fuel cell
JP2007087860A (en) * 2005-09-26 2007-04-05 Equos Research Co Ltd Cell and stack of fuel cell

Also Published As

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