JPH0160903B2 - - Google Patents

Info

Publication number
JPH0160903B2
JPH0160903B2 JP58119801A JP11980183A JPH0160903B2 JP H0160903 B2 JPH0160903 B2 JP H0160903B2 JP 58119801 A JP58119801 A JP 58119801A JP 11980183 A JP11980183 A JP 11980183A JP H0160903 B2 JPH0160903 B2 JP H0160903B2
Authority
JP
Japan
Prior art keywords
air
reaction
manifold
cooling
stack
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.)
Expired
Application number
JP58119801A
Other languages
Japanese (ja)
Other versions
JPS6012673A (en
Inventor
Masao Kumeta
Kensho Matsuoka
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP58119801A priority Critical patent/JPS6012673A/en
Priority to US06/528,443 priority patent/US4508793A/en
Publication of JPS6012673A publication Critical patent/JPS6012673A/en
Publication of JPH0160903B2 publication Critical patent/JPH0160903B2/ja
Granted legal-status Critical Current

Links

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
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04014Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
    • 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

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

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は空冷式燃料電池、特に冷却空気と反応
空気とを分離供給する方式の燃料電池に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to an air-cooled fuel cell, and particularly to a fuel cell in which cooling air and reaction air are separately supplied.

(ロ) 従来技術 りん酸電解液燃料電池は、180℃〜200℃の作動
温度を維持するため冷却が必要である。空冷方式
としては、共通マニホルドに送られた空気を反応
空気及び冷却空気として各通路に分配する方法
と、反応空気とは分離して冷却空気を供給する方
法とがある。
(b) Prior Art Phosphoric acid electrolyte fuel cells require cooling to maintain an operating temperature of 180°C to 200°C. Air cooling methods include a method in which air sent to a common manifold is distributed to each passage as reaction air and cooling air, and a method in which cooling air is supplied separately from reaction air.

前者は反応水素ガス通路を含めて前記各通路の
パターンが簡単であるという利点を有するが、反
応及び冷却に夫々必要とされる空気量を各通路に
配分することがむつかしく、電池反応と電池温度
のバランスがくづれて電池特性上好ましくない。
The former has the advantage that the pattern of each passage including the reaction hydrogen gas passage is simple, but it is difficult to allocate the amount of air required for reaction and cooling to each passage, and the battery reaction and battery temperature are The balance is disrupted, which is unfavorable in terms of battery characteristics.

一方後者は第1図、第2図のようなスタツクイ
とマニホルドロを用いて反応空気と冷却空気を分
離供給するため、各通路のパターンが複雑で流通
抵抗が大きくなり、大容量のブロワを必要とする
などの欠点があつた。
On the other hand, in the latter case, reaction air and cooling air are separately supplied using a static screw and a manifold drawer as shown in Figures 1 and 2, so the pattern of each passage is complex, resulting in high flow resistance and the need for a large-capacity blower. There were drawbacks such as:

本出願人はかかる点に鑑み、冷却空気と反応空
気を共通に供給する方式の電池スタツクにわづか
の改良を加えることにより、冷却空気と反応空気
とを分離供給できるようにした燃料電池を提案し
た。(特願昭57−157133号) 前記提案電池は、第3図、第4図に示すよう
に、電池スタツク1に介在する各冷却板2をスタ
ツクの空気流通面より突設してスタツクに取付け
た反応空気用マニホルド3の窓口4に気密的に装
着し、各窓口4に露出する冷却空気通路5を、反
応空気用マニホルド3上に取付けた冷却空気用マ
ニホルド6内に連通させたものである。
In view of this, the present applicant has proposed a fuel cell that is capable of separately supplying cooling air and reaction air by making slight improvements to a cell stack that commonly supplies cooling air and reaction air. did. (Japanese Patent Application No. 57-157133) As shown in FIGS. 3 and 4, the proposed battery is attached to the stack by having each cooling plate 2 interposed in the battery stack 1 protrude from the air circulation surface of the stack. The cooling air passage 5 exposed at each window 4 is connected to the inside of the cooling air manifold 6 installed on the reaction air manifold 3. .

この場合反応空気用マニホルド3内は、各突設
冷却板2′で区隔されるので、このマニホルド3
の一側面に、各冷却板2間のサブスタツク1′に
対応する開口7を設けると共にこれら開口7を覆
う補助マニホルド8を取付ける。尚スタツク1の
水素流通面には通常の如く水素ガス用マニホルド
9を有する。
In this case, the inside of the reaction air manifold 3 is separated by each protruding cooling plate 2', so the inside of the reaction air manifold 3 is
Openings 7 corresponding to the substack 1' between each cooling plate 2 are provided on one side of the cooling plate 2, and an auxiliary manifold 8 is attached to cover these openings 7. The hydrogen flow surface of the stack 1 is provided with a hydrogen gas manifold 9 as usual.

従つて反応空気は、補助マニホルド8を経て各
開口7よりサブスタツクの各反応空気通路に対し
て直角方向に供給されるため、空気流通方向に配
列する各通路に均一に導入され難い。即ち供給空
気量が多い場合さほど問題とならないが、供給量
が多くない場合各開口7より遠ざかる反応空気通
路ほぼ導入量が大きくなる傾向を示し、電池反応
の不均一により特性に悪影響を与える。この不均
一解消のために追加分の空気を送ることはそれだ
けブロワの負担となつて効率を損うなどの問題が
あつた。
Therefore, the reaction air is supplied from each opening 7 through the auxiliary manifold 8 in a direction perpendicular to each reaction air passage of the substack, and therefore it is difficult to uniformly introduce the reaction air into each passage arranged in the air flow direction. That is, if the amount of supplied air is large, this is not a big problem, but if the amount of supplied air is not large, the reaction air passages that are farther away from each opening 7 tend to introduce a larger amount of air, which adversely affects the characteristics of the battery due to non-uniformity of the reaction. Sending an additional amount of air to eliminate this non-uniformity places a corresponding burden on the blower, resulting in problems such as loss of efficiency.

(ハ) 発明の目的 本発明の目的は簡単な構成をもつ冷却空気分離
方式の燃料電池を提供することであり、特に前記
問題点を解消して反応空気の各通路への供給を均
一化して電池特性を改善することである。
(c) Purpose of the Invention The purpose of the present invention is to provide a cooling air separation type fuel cell having a simple configuration, and in particular, to solve the above-mentioned problems and uniformly supply reaction air to each passage. The goal is to improve battery characteristics.

(ニ) 発明の構成 本発明は電池スタツクの空気流通面に、反応空
気用マニホルドと冷却空気用マニホルドとを順次
重合装着し、前記スタツクに介在する各冷却板を
前記空気流通面より突設してその冷却空気通路を
冷却空気用マニホルドに連通させた方式の燃料電
池であつて、前記突設冷却板で区隔された前記反
応空気用マニホルド内に、各サブスタツクに対応
して、多数の空気吹出口を有する有底パイプを
夫々延設せしめたことを特徴とする。
(d) Structure of the Invention The present invention comprises sequentially superimposing a reaction air manifold and a cooling air manifold on the air circulation surface of a battery stack, and each cooling plate interposed in the stack is provided to protrude from the air circulation surface. The fuel cell is of a type in which a cooling air passage is communicated with a cooling air manifold, and a large number of air reactors are provided in the reaction air manifold separated by the protruding cooling plates, corresponding to each substack. It is characterized by extending bottomed pipes each having an air outlet.

又本発明の他の特徴は、前記反応空気用マニホ
ルドの一側面に、前記パイプに連通する補助マニ
ホルドを取付けた点及び前記パイプの空気吹出口
が前記反応空気用マニホルド内面に向つて開口し
ている点に在る。更に本発明は、前記スタツク内
の反応空気流及び冷却空気流が互に対向流となる
よう構成したことを特徴とする。
Another feature of the present invention is that an auxiliary manifold communicating with the pipe is attached to one side of the reaction air manifold, and an air outlet of the pipe opens toward the inner surface of the reaction air manifold. Be at the point where you are. Furthermore, the present invention is characterized in that the reaction air flow and the cooling air flow within the stack are configured to flow in opposite directions.

(ホ) 実施例 本発明による電池スタツク1は陰陽ガス極間に
電解液含浸マトリツクスを介挿した単位セルと、
両面に互に交錯する方向の各反応ガス(水素ガス
及び空気)通路を配列した炭素質ガス分離板とを
交互に多数積重し、4〜5単位セル(サブスタツ
ク)毎に、空気通路5を有する炭素質冷却板2を
介在させて上下端板間で締付けられる。
(E) Example A battery stack 1 according to the present invention includes a unit cell in which an electrolyte-impregnated matrix is inserted between negative and positive gas electrodes,
A large number of carbonaceous gas separation plates each having reaction gas (hydrogen gas and air) passages arranged in intersecting directions on both sides are stacked alternately, and air passages 5 are arranged in every 4 to 5 unit cells (substack). The upper and lower end plates are tightened with a carbonaceous cooling plate 2 interposed therebetween.

このスタツク構成は、反応空気と冷却空気とを
共通的に供給する所謂ダイガスシステムと同様で
あるが、本発明では各冷却板2をスタツクの空気
流通面より突設して冷却空気用マニホルド6と連
通させて冷却分離方式とした。
This stack configuration is similar to a so-called die gas system that commonly supplies reaction air and cooling air, but in the present invention, each cooling plate 2 is provided protruding from the air circulation surface of the stack to form a cooling air manifold 6. The cooling separation method was adopted by communicating with the

この場合、反応空気用マニホルド3内は、前記
突設冷却板2′により、各サブスタツク1′の空気
流通面に対応した隔室Aに区分されるが、これら
各隔室Aの長手方向には、第5図及び第6図に示
すように、各開口7より多数の空気吹出口10′
を有する有底パイプ10が延設される。
In this case, the interior of the reaction air manifold 3 is divided into compartments A corresponding to the air flow surfaces of each substack 1' by the protruding cooling plate 2', but the longitudinal direction of each compartment A is , as shown in FIGS. 5 and 6, each opening 7 has a large number of air outlets 10'.
A bottomed pipe 10 is extended.

これらパイプ10の一端は、予め有底とする代
りに反応空気用マニホルド3の側壁内面で閉塞し
てもよく、パイプ10の他端は補助マニホルド8
内に開口している。各パイプ10の空気吹出口1
0′は、約2cm間隔で反応空気用マニホルド3内
面に向つて開口し、吹出空気が第6図の矢印に示
すように一旦マニホルド内壁に当つてサブスタツ
ク1′の各反応空気溝に供給される。
One end of these pipes 10 may be closed with the inner surface of the side wall of the reaction air manifold 3 instead of having a bottom in advance, and the other end of the pipe 10 is connected to the auxiliary manifold 8.
It is open inward. Air outlet 1 of each pipe 10
0' opens toward the inner surface of the reaction air manifold 3 at intervals of about 2 cm, and the blown air once hits the inner wall of the manifold as shown by the arrow in Fig. 6, and is supplied to each reaction air groove of the substack 1'. .

更に空気吹出口10′の口径は、すべて等しく
すれば、空気圧のためパイプ入口からはなれる程
吹出量が大きくなつて、各反応空気溝への空気供
給量が不均一となるので、流通方向に向つて順次
小さくなるよう12mmφ〜7mmφの範囲に穿設す
る。パイプ10の材質としては、耐熱、耐酸性を
考慮してステンレスもしくはカーボンとする。
Furthermore, if the diameters of the air outlet ports 10' are all the same, the air pressure will cause the outlet amount to increase the further away from the pipe inlet, and the amount of air supplied to each reaction air groove will become uneven. The holes are drilled in the range of 12 mmφ to 7 mmφ so that the diameter decreases gradually. The material of the pipe 10 is stainless steel or carbon in consideration of heat resistance and acid resistance.

電池スタツク1は反応空気の入口側(約150℃)
より出口側(約180℃)に向つて高温となるので、
冷却空気は、反応空気の出口側より供給すれば、
スタツク内の温度勾配を低減することができる。
Battery stack 1 is on the reaction air inlet side (approximately 150℃)
Since the temperature becomes higher towards the outlet side (approximately 180℃),
If cooling air is supplied from the outlet side of the reaction air,
Temperature gradients within the stack can be reduced.

従つて入口側(出口側)の反応空気用マニホル
ド3上には出口側(入口側)の冷却空気用マニホ
ルド6を取付け、第6図に示すようにスタツク内
の反応空気流(←)と冷却空気流(〓)が対向流
となるよう構成する。
Therefore, the cooling air manifold 6 on the outlet side (inlet side) is installed on the reaction air manifold 3 on the inlet side (outlet side), and as shown in FIG. The airflow (〓) is configured to be a counterflow.

尚出口側反応空気用マニホルド3内には、前記
の如きパイプ10を設ける必要はなく、このマニ
ホルド側壁に、各サブスタツク1′に対応する出
口を穿設するだけでよい。
It is not necessary to provide the pipe 10 as described above in the outlet-side reaction air manifold 3, and it is sufficient to simply provide an outlet corresponding to each substack 1' in the side wall of the manifold.

(ホ) 発明の効果 本発明によれば、反応空気と冷却空気とを共通
化した電池スタツクにわづかの修正を加えること
により、冷却空気分離方式とすることができるの
で、従来の分離方式に比し各ガス通路のパターン
が極めて単純でガス分離板及び冷却板の作成が簡
単化される。
(E) Effects of the Invention According to the present invention, by making slight modifications to the battery stack that uses common reaction air and cooling air, it is possible to create a cooling air separation system. In comparison, the pattern of each gas passage is extremely simple, and the fabrication of the gas separation plate and cooling plate is simplified.

又電池スタツクに介在する冷却板より突設した
部分が反応空気用マニホルド内を区隔し、この各
隔室内に多数の空気吹出口を有するパイプを延在
させているので、各サブスタツクの反応空気通路
へ円滑に反応空気を導入することができ、特に空
気吹出口をマニホルド内面に向つて開口させれ
ば、吹出空気がサブスタツク上下方向の反応空気
通路に均一に分配されると共に空気吹出口の口径
をパイプ入口側より順次小さくすれば、吹出空気
がサブスタツク左右方向の反応空気通路に均一に
分配され、配分量の不均一による特性劣化を防止
することができる。
In addition, a portion protruding from the cooling plate interposed in the battery stack partitions the inside of the reaction air manifold, and a pipe with a large number of air outlets extends within each compartment, so that the reaction air of each substack is Reaction air can be smoothly introduced into the passage, and in particular, if the air outlet is opened toward the inner surface of the manifold, the blown air can be uniformly distributed to the reaction air passages in the vertical direction of the substack, and the diameter of the air outlet can be smoothly introduced. By making the amount smaller sequentially from the pipe inlet side, the blown air is evenly distributed to the reaction air passages in the left and right directions of the substack, and it is possible to prevent characteristic deterioration due to uneven distribution.

更にスタツク内の冷却空気流と反応空気流とを
対向流として流通させれば、スタツクの温度勾配
を均一化して電池寿命を向上することが可能とな
るなどすぐれた効果を発揮する。
Furthermore, if the cooling air flow and the reaction air flow in the stack are made to flow in opposite directions, excellent effects such as making it possible to equalize the temperature gradient in the stack and improving the battery life can be achieved.

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

第1図、第2図はいずれも従来の分離冷却経路
を有する空冷式燃料電池の平面図である。第3図
乃至第6図は本発明燃料電池を示し、第3図は一
部分解斜面図、第4図は同上電池スタツクの斜面
図、第5図は同上の要部拡大斜面図、第6図は同
じく要部拡大断面図である。 1…電池スタツク、1′…サブスタツク、2…
冷却板、2′…冷却板突設部、3…反応空気用マ
ニホルド、5…冷却空気通路、6…冷却空気用マ
ニホルド、8…補助マニホルド、9…反応水素用
マニホルド、10…パイプ、10′…空気吹出口、
A…隔室。
FIG. 1 and FIG. 2 are both plan views of a conventional air-cooled fuel cell having separate cooling paths. 3 to 6 show the fuel cell of the present invention, FIG. 3 is a partially exploded slope view, FIG. 4 is a slope view of the same battery stack, FIG. 5 is an enlarged slope view of the main parts of the same, and FIG. is also an enlarged sectional view of the main part. 1...Battery stack, 1'...Sub stack, 2...
Cooling plate, 2'...Cooling plate protrusion, 3...Reaction air manifold, 5...Cooling air passage, 6...Cooling air manifold, 8...Auxiliary manifold, 9...Reaction hydrogen manifold, 10...Pipe, 10' ...air outlet,
A...Separate room.

Claims (1)

【特許請求の範囲】 1 冷却通路が形成された多数の冷却板を含む電
池スタツクを備えた空冷式燃料電池において、前
記各冷却板は反応空気流通面に前記冷却通路が開
口した突設部を有し、該突設部が前記電池スタツ
クに取付けた反応空気用マニホルドを気密的に貫
通すると共に反応空気用マニホルド上に設けた冷
却空気用マニホルド内に連通しており、前記冷却
板突設部で区隔された前記反応空気用マニホルド
内に、各冷却板間のサブスタツクに対応して、多
数の空気吹出口を有するパイプを反応空気用マニ
ホルドの一側面開口より延設し、前記各パイプに
連通する補助マニホルドを反応空気用マニホルド
の前記一側面に取付けたことを特徴とする空冷式
燃料電池。 2 前記パイプの空気吹出口は、前記反応空気用
マニホルド内壁に向つて開口していることを特徴
とする特許請求の範囲第1項記載の空冷式燃料電
池。 3 前記電池スタツク内における反応空気流と冷
却空気流とが互に対向流となるよう構成したこと
を特徴とする特許請求の範囲第1項記載の空冷式
燃料電池。
[Scope of Claims] 1. In an air-cooled fuel cell equipped with a cell stack including a plurality of cooling plates each having a cooling passage formed therein, each of the cooling plates has a protruding portion in which the cooling passage is opened on a reaction air circulation surface. The protruding portion airtightly penetrates the reaction air manifold attached to the battery stack and communicates with the inside of the cooling air manifold provided on the reaction air manifold, and the cooling plate protruding portion In the reaction air manifold separated by , pipes each having a large number of air outlets are installed from an opening on one side of the reaction air manifold, corresponding to the sub-stack between each cooling plate, and each pipe has a plurality of air outlets. An air-cooled fuel cell characterized in that a communicating auxiliary manifold is attached to the one side of the reaction air manifold. 2. The air-cooled fuel cell according to claim 1, wherein the air outlet of the pipe opens toward the inner wall of the reaction air manifold. 3. The air-cooled fuel cell according to claim 1, wherein the reaction air flow and the cooling air flow within the cell stack are configured to flow in opposite directions.
JP58119801A 1982-09-08 1983-06-30 Air cooling type fuel cell Granted JPS6012673A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP58119801A JPS6012673A (en) 1983-06-30 1983-06-30 Air cooling type fuel cell
US06/528,443 US4508793A (en) 1982-09-08 1983-09-01 Air-cooled fuel cell system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58119801A JPS6012673A (en) 1983-06-30 1983-06-30 Air cooling type fuel cell

Publications (2)

Publication Number Publication Date
JPS6012673A JPS6012673A (en) 1985-01-23
JPH0160903B2 true JPH0160903B2 (en) 1989-12-26

Family

ID=14770557

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58119801A Granted JPS6012673A (en) 1982-09-08 1983-06-30 Air cooling type fuel cell

Country Status (1)

Country Link
JP (1) JPS6012673A (en)

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* Cited by examiner, † Cited by third party
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US7135247B2 (en) * 2003-10-23 2006-11-14 Utc Fuel Cells, Llc Easily isolated, oversized fuel cell stack cooler plates
JP2014056836A (en) * 2013-11-15 2014-03-27 Toto Ltd Fuel battery

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