JPH04324254A - Generating unit provided with differential pressure adjusting device - Google Patents

Generating unit provided with differential pressure adjusting device

Info

Publication number
JPH04324254A
JPH04324254A JP3095246A JP9524691A JPH04324254A JP H04324254 A JPH04324254 A JP H04324254A JP 3095246 A JP3095246 A JP 3095246A JP 9524691 A JP9524691 A JP 9524691A JP H04324254 A JPH04324254 A JP H04324254A
Authority
JP
Japan
Prior art keywords
fuel
pressure
oxidizing gas
duct
gas
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.)
Withdrawn
Application number
JP3095246A
Other languages
Japanese (ja)
Inventor
Hiroshi Yoshida
弘 吉田
Toshio Inoue
俊夫 井上
Yoshimi Ezaki
江崎 義美
Masatoshi Hattori
服部 雅俊
Mitsuhiro Irino
光博 入野
Kazuhisa Tanaka
田中 量久
Toshio Haneda
羽田 壽夫
Koichi Takenobu
弘一 武信
Fusayuki Nanjo
房幸 南條
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.)
Chubu Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
Original Assignee
Chubu Electric Power Co Inc
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 Chubu Electric Power Co Inc, Mitsubishi Heavy Industries Ltd filed Critical Chubu Electric Power Co Inc
Priority to JP3095246A priority Critical patent/JPH04324254A/en
Publication of JPH04324254A publication Critical patent/JPH04324254A/en
Withdrawn legal-status Critical Current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

Landscapes

  • Fuel Cell (AREA)

Abstract

PURPOSE:To suppress leakage of oxidizing gas from a sealing gasket of a fuel cell by adjusting a position of a partitioning plate, provided in a residual fuel duct, through a partitioning plate driving gear by a drive control unit so that a pressure of fuel gas in the fuel duct can be increased to the pressure suited for a pressure in an oxidizing gas flow passage. CONSTITUTION:Detection signals, respectively output from a fuel gas pressure detector 55 arranged in an oxidizing gas flow passage 41a and an oxidizing gas pressure detector 56 arranged in a fuel duct 12, are input to a drive control unit 54 which feeds a pressure of liquid to a gate valve driving gear 53 through a switching valve. The gate valve driving gear 53, which drives a partitioning plate 51 for opening/closing a residual fuel gas duct 52, adjusts a position of the gate valve 51, so that a pressure of the fuel gas pressure detector 55 is generated equal to a pressure of the oxidizing gas pressure detector 56, to minimize leakage to the fuel duct 12 of oxidizing gas 4 from a sealing gasket 8 of a fuel cell 9. In this way, a fuel gas pressure in the fuel duct can be increased to a value suited for a pressure of the oxidizing gas flow passage.

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、水素ガスや天然ガス等
を使用する平板型固体電解質燃料電池が適用される差圧
調整装置を備えた発電装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a power generating apparatus equipped with a differential pressure regulating device to which a flat solid electrolyte fuel cell using hydrogen gas, natural gas, etc. is applied.

【0002】0002

【従来の技術】平板型固体電解質電池を用いた発電装置
としては、本出願人の一人の先願に係る特許出願(出願
番号「平成2年特許願第083864号、発明の名称「
発電装置」)がある。
[Prior Art] As a power generation device using a flat solid electrolyte battery, a patent application related to an earlier application by one of the present applicants (application number: 1990 Patent Application No. 083864, title of invention:
There is a "power generation device").

【0003】前記本出願人の一人の特許出願に係る発電
装置に用いる平板型固体電解質燃料電池9は、図3及び
図4に示すように上面通路壁であるインタコネクタ11
と下面通路壁である電圧発生部支持枠10の間に形成さ
れた燃料ガス通路2を有する。図中の7は酸化ガス通路
であり、上面壁である電圧発生部支持枠10と、下面通
路壁であるインタコネクタ11の間に形成されている。 前記インタコネクタ11と電圧発生部支持枠10は積層
されている。この上下両面には、それぞれ前記酸化ガス
導管5及び残存酸化ガス導管36を固着した継ぎフラン
ジ34が取付けられている。前記電圧発生部支持枠10
、インタコネクタ11及び継ぎフランジ34間は、シー
ル用ガスケット8によって遮蔽されている。なお、前記
酸化ガス導管5と酸化ガス通路7の間には酸化ガス4を
各酸化ガス通路7に分配するための酸化ガス用マニホー
ルド6が、前記酸化ガス通路7と残存酸化ガス導管36
の間には、分配された電池反応後の残存酸化ガス18を
集めるための酸化ガス用マニホールド6が、それぞれ形
成されている。
[0003] A flat solid electrolyte fuel cell 9 used in a power generation device according to a patent application filed by one of the present applicants has an interconnector 11 which is an upper passage wall, as shown in FIGS. 3 and 4.
The fuel gas passage 2 is formed between the fuel gas passage 2 and the voltage generator support frame 10, which is a lower passage wall. Reference numeral 7 in the figure indicates an oxidizing gas passage, which is formed between the voltage generator support frame 10, which is the upper wall, and the interconnector 11, which is the lower passage wall. The interconnector 11 and the voltage generator support frame 10 are stacked. Joint flanges 34 to which the oxidizing gas conduit 5 and residual oxidizing gas conduit 36 are fixed are attached to both the upper and lower surfaces. The voltage generator support frame 10
, the interconnector 11 and the joint flange 34 are shielded by a sealing gasket 8. An oxidizing gas manifold 6 is provided between the oxidizing gas conduit 5 and the oxidizing gas passage 7 for distributing the oxidizing gas 4 to each oxidizing gas passage 7.
Oxidizing gas manifolds 6 for collecting the distributed oxidizing gas 18 remaining after the cell reaction are formed between them.

【0004】なお、前述した発電装置の断熱部材、耐火
材等は全てセラミックスから形成されて1000℃以上
の高温に耐えられるようになっており、かつ燃料電池9
の固体電解質もセラミックスから形成されている。
[0004] The heat insulating members, refractory materials, etc. of the above-mentioned power generation device are all made of ceramics so that they can withstand high temperatures of 1000°C or more, and the fuel cell 9
The solid electrolyte of is also formed from ceramics.

【0005】前記燃料電池9を内蔵する発電装置の一例
について、図5により以下に説明する。図5において、
31は上下の断熱部材(あるいは耐火材)及び側部の耐
火材で区画された排ガス室である。この排ガス室31に
は、燃料電池収納室35が気密隔壁32cを介して配置
されている。前記燃料電池収納室35の側部には、板状
耐火材32dが配置され、かつ該板状耐火材32dとの
間には前記気密隔壁32cが介装されている。前記板状
耐火材32d中間部には、残存燃料ガスダクト52が形
成されている。
An example of a power generation device incorporating the fuel cell 9 will be explained below with reference to FIG. In Figure 5,
31 is an exhaust gas chamber partitioned by upper and lower heat insulating members (or fireproof materials) and fireproof materials on the sides. A fuel cell storage chamber 35 is arranged in the exhaust gas chamber 31 via an airtight partition wall 32c. A plate-shaped refractory material 32d is arranged on the side of the fuel cell storage chamber 35, and the airtight partition wall 32c is interposed between the plate-shaped refractory material 32d and the plate-shaped refractory material 32d. A residual fuel gas duct 52 is formed in the intermediate portion of the plate-shaped refractory material 32d.

【0006】前記燃料電池収納室35内の前記排ガス室
31側の板状耐火材32d上には、アフタバーナ16が
、該アフタバーナ16と反対側の耐火材上には燃料ガス
導管14がそれぞれ設置されている。気密隔壁32a〜
32cの外側又は両側に空冷管(又は水冷管)40を配
置しており、燃料電池9上には、シールガスケット用重
し20が載置されている。なお、図中の12は燃料ダク
トである。前記シールガスケット用重し20には、前記
燃料電池9に酸化ガスを供給するための非導電性セラミ
ックス製の複数の酸化ガス流通路41がそれぞれ挿着さ
れている。前記各燃料電池9には残存ガスダクト30に
達する残存酸化ガス導管36がそれぞれ貫通されている
[0006] An afterburner 16 is installed on the plate-shaped refractory material 32d on the side of the exhaust gas chamber 31 in the fuel cell storage chamber 35, and a fuel gas conduit 14 is installed on the refractory material on the opposite side of the afterburner 16. ing. Airtight bulkhead 32a~
An air-cooled pipe (or water-cooled pipe) 40 is disposed outside or on both sides of the fuel cell 9, and a seal gasket weight 20 is placed on the fuel cell 9. Note that 12 in the figure is a fuel duct. A plurality of oxidizing gas flow passages 41 made of non-conductive ceramics for supplying oxidizing gas to the fuel cell 9 are inserted into each of the seal gasket weights 20 . A residual oxidant gas conduit 36 extending to the residual gas duct 30 passes through each of the fuel cells 9 .

【0007】前記排ガス室31内には蛇行した酸化ガス
予熱用熱交換器17が配置されている。この熱交換器1
7の一端側は、図示されていない酸化ガス導入管が連結
されている。前記熱交換器17とバーナ16の間には、
耐火材26が設けられている。前記熱交換器17の他端
は、前記排ガス室31の上壁付近を通り気密隔壁を貫通
して酸化ガス流通路41に終端している。流通路41の
他端付近には、これら流通路41から分岐した流通路4
1に連結され酸化ガス導管を構成している。前記流通路
41の他端には起動用バーナ22が連結されている。な
お、起動用バーナ22の周囲は断熱材で覆われている。 前記起動用バーナ22には、点火装置22a、燃料ガス
供給管22c及び酸化ガス供給管22bが付設されてい
る。前記排ガス室31を区画する断熱材の左壁には、煙
突に繋がる排ガス管37が設けられている。
A meandering oxidizing gas preheating heat exchanger 17 is disposed within the exhaust gas chamber 31. This heat exchanger 1
One end of 7 is connected to an oxidizing gas introduction pipe (not shown). Between the heat exchanger 17 and the burner 16,
A refractory material 26 is provided. The other end of the heat exchanger 17 passes near the upper wall of the exhaust gas chamber 31, penetrates the airtight partition wall, and terminates in the oxidizing gas flow passage 41. Near the other end of the flow passages 41, there are flow passages 4 branched from these flow passages 41.
1 to constitute an oxidizing gas conduit. A starting burner 22 is connected to the other end of the flow path 41 . Note that the starting burner 22 is covered with a heat insulating material. The starting burner 22 is provided with an ignition device 22a, a fuel gas supply pipe 22c, and an oxidizing gas supply pipe 22b. An exhaust gas pipe 37 connected to a chimney is provided on the left wall of the heat insulating material that partitions the exhaust gas chamber 31.

【0008】次に、前述した構成の発電装置の作用を起
動運転時と定常運転時とに分けて説明する。
[0008] Next, the operation of the power generating apparatus having the above-mentioned configuration will be explained separately during startup operation and during steady operation.

【0009】起動運転時については、燃料ガス導入管1
4より導入された燃料ガス1(H2 ガスや天然ガス)
は、燃料ダクト12を通って各平板型固体電解質燃料電
池9に供給される。一方、排ガス室31に導設された図
示しない酸化ガス導入管より供給された酸化ガス4(空
気)は、酸化ガス予熱用熱交換器17、酸化ガス流通路
41を通して各燃料電池に供給され、後述する作用によ
り発電がなされる。
During start-up operation, the fuel gas introduction pipe 1
Fuel gas 1 (H2 gas or natural gas) introduced from 4
is supplied to each flat solid electrolyte fuel cell 9 through the fuel duct 12. On the other hand, oxidizing gas 4 (air) supplied from an oxidizing gas introduction pipe (not shown) led to the exhaust gas chamber 31 is supplied to each fuel cell through the oxidizing gas preheating heat exchanger 17 and the oxidizing gas flow path 41, Power is generated by the action described below.

【0010】発電後、酸化ガス4は残存酸化ガス18と
なって残存酸化ガス導管36、残存酸化ガスダクト30
を通って前記排ガス室31に流入し、耐火材26によっ
て上方に案内される。一方、残存燃料ガス15は前記残
存燃料ガスダクト52を通って前記排ガス室31に流入
する。ここで、残存燃料ガス15と残存酸化ガス18を
アフタバーナ16により再燃焼させることにより、前記
排ガス室31に配置された蛇行する酸化ガス予熱用熱交
換器17を加熱することにより該熱交換器17内を通る
酸化ガス4を予熱する。再燃焼したガス38は、排ガス
管37を通って煙突より排出される。
After power generation, the oxidizing gas 4 becomes a residual oxidizing gas 18 and is transferred to a residual oxidizing gas conduit 36 and a residual oxidizing gas duct 30.
through which it flows into the exhaust gas chamber 31 and is guided upwards by the refractory material 26. On the other hand, the remaining fuel gas 15 flows into the exhaust gas chamber 31 through the remaining fuel gas duct 52. Here, the residual fuel gas 15 and the residual oxidant gas 18 are re-combusted by the afterburner 16 to heat the meandering oxidant gas preheating heat exchanger 17 disposed in the exhaust gas chamber 31. The oxidizing gas 4 passing through is preheated. The reburned gas 38 passes through the exhaust gas pipe 37 and is discharged from the chimney.

【0011】上述した発電装置の起動時において、10
00℃という高温の反応温度に到達するには時間を要す
る。このため、起動用バーナ22により複数の酸化ガス
流通路41に供給する酸化ガス4を加熱し、これと燃料
ガス1を反応させることにより、前記各平板型固体電解
質燃料電池9を定格温度に到達させる。この際、前述し
たように残存燃料ガス15と残存酸化ガス18をアフタ
バーナ16により再燃焼させることにより、前記排ガス
室31に配置された蛇行する酸化ガス予熱用熱交換器1
7は加熱され、該熱交換器17内を通る酸化ガス4を予
熱し、該予熱された酸化ガス4を酸化ガス流通路41を
通して各燃料電池9に供給することによって、燃料電池
9の反応速度を促進し、起動時間の短縮化を図ることが
できる。
[0011] At the time of starting up the above-mentioned power generation device, 10
It takes time to reach a reaction temperature as high as 00°C. Therefore, by heating the oxidizing gas 4 supplied to the plurality of oxidizing gas flow passages 41 by the starting burner 22 and causing the fuel gas 1 to react with the oxidizing gas 4, each of the flat solid electrolyte fuel cells 9 reaches the rated temperature. let At this time, the residual fuel gas 15 and the residual oxidant gas 18 are re-combusted by the afterburner 16 as described above, so that the meandering oxidant gas preheating heat exchanger 1 disposed in the exhaust gas chamber 31
7 is heated to preheat the oxidizing gas 4 passing through the heat exchanger 17, and supplying the preheated oxidizing gas 4 to each fuel cell 9 through the oxidizing gas flow path 41, thereby increasing the reaction rate of the fuel cell 9. It is possible to promote this and shorten the startup time.

【0012】定常運転時においては、反応温度が定格温
度に達すると、起動用バーナ22を停止し、その後は酸
化ガス4及び燃料ガス1を継続して供給することにより
、自立した発電装置として作動する。
During steady operation, when the reaction temperature reaches the rated temperature, the starting burner 22 is stopped, and thereafter the oxidizing gas 4 and the fuel gas 1 are continuously supplied, thereby operating as an independent power generating device. do.

【0013】次に、前記の平板型固体電解質燃料電池9
の作用について、図3乃至図5により説明する。
Next, the above-mentioned flat plate solid electrolyte fuel cell 9
The operation will be explained with reference to FIGS. 3 to 5.

【0014】燃料ダクト12を通して導入された燃料ガ
ス1は、燃料ガス通路2に供給され、電圧発生部支持枠
10の上面を流れる。一方、酸化ガス流通路41から導
入された酸化ガス4は酸化ガス用内部マニホールド6に
て各々の酸化ガス通路7に分配され、電圧発生部支持枠
10の下面を流れ、このとき電流が流れる。この電流を
上下の継ぎフランジ34に接続された電流リード21か
ら取り出す。
The fuel gas 1 introduced through the fuel duct 12 is supplied to the fuel gas passage 2 and flows on the upper surface of the voltage generator support frame 10 . On the other hand, the oxidizing gas 4 introduced from the oxidizing gas flow passage 41 is distributed to each oxidizing gas passage 7 by the oxidizing gas internal manifold 6 and flows under the voltage generator support frame 10, at which time a current flows. This current is taken out from the current lead 21 connected to the upper and lower joint flanges 34.

【0015】なお、上記においては、酸化ガス4を予熱
する酸化ガス予熱用熱交換器17及び酸化ガス導管に起
動用バーナ22を設けた例を説明したが、排ガス室31
に酸化ガス予熱用熱交換器17と燃料ガスを予熱する燃
料ガス予熱用熱交換器を設け、かつ前記酸化ガス導管に
起動バーナ22を設ける代わりに燃料ガス導入管14に
立上げ用の起動バーナを設けた場合も作用は同じである
。また、酸化ガス及び燃料ガスの予熱用熱交換器はフイ
ン付管としてもよい。
[0015] In the above, an example has been described in which the oxidizing gas preheating heat exchanger 17 for preheating the oxidizing gas 4 and the starting burner 22 are provided in the oxidizing gas conduit.
A heat exchanger 17 for preheating the oxidizing gas and a heat exchanger for preheating the fuel gas for preheating the fuel gas are provided in the oxidizing gas conduit, and instead of providing the starting burner 22 in the oxidizing gas conduit, a starting burner for starting up is provided in the fuel gas introduction pipe 14. The effect is the same even if . Further, the heat exchanger for preheating the oxidizing gas and the fuel gas may be a finned tube.

【0016】[0016]

【発明が解決しようとする課題】本出願人の一人の先願
に係る発電装置においては、図4に示すように酸化ガス
4は酸化ガス導管5、酸化ガス用内部マニホールド6、
酸化ガス通路7、残存酸化ガス導管36と流れる。一方
、燃料ガス1は図3に示すように燃料ガス通路2を通過
するのみである。
In the power generation device according to the earlier application of one of the present applicants, as shown in FIG.
It flows through the oxidizing gas passage 7 and the residual oxidizing gas conduit 36 . On the other hand, the fuel gas 1 only passes through the fuel gas passage 2 as shown in FIG.

【0017】一般に、酸化ガス4は燃料ガス1に比較し
多量に流す必要があり、さらに、酸化ガス通路は前述の
ように曲折していることもあり流れの圧損が大きい。し
たがって、燃料電池を組み込んだ図5に示す発電装置で
は、酸化ガス流通路41の圧力は燃料ダクト12の圧力
に比べ数10〜数100mmAg高くなる。
Generally, it is necessary to flow the oxidizing gas 4 in a larger amount than the fuel gas 1, and furthermore, since the oxidizing gas passage is curved as described above, the pressure drop in the flow is large. Therefore, in the power generating apparatus shown in FIG. 5 incorporating the fuel cell, the pressure in the oxidizing gas flow path 41 is higher than the pressure in the fuel duct 12 by several tens to hundreds of mmAg.

【0018】この両ガス間の圧力差は酸化ガス通路7と
燃料ガス通路2の差圧および燃料ダクト12(または燃
料電池収納室35)と酸化ガス通路7間の差圧となり、
シール用ガスケット8からの酸化ガス4の燃料ガス側へ
の漏洩の原因となるおそれがあり、その改善が望まれて
いた。
The pressure difference between the two gases becomes the differential pressure between the oxidizing gas passage 7 and the fuel gas passage 2 and the differential pressure between the fuel duct 12 (or fuel cell storage chamber 35) and the oxidizing gas passage 7,
There is a possibility that the oxidizing gas 4 leaks from the sealing gasket 8 to the fuel gas side, and an improvement has been desired.

【0019】本発明は上記の課題を解決しようとするも
のである。
The present invention aims to solve the above problems.

【0020】[0020]

【課題を解決するための手段】本発明の差圧調整装置を
備えた発電装置は、燃料ダクトと酸化ガス流通路が接続
され残存燃料ガスダクトに接続され電圧発生部支持枠と
インタコネクタがシール用ガスケットを介して積層され
た燃料電池を備えた発電装置において、上記残存燃料ガ
スダクトに設けられ同ダクトを開閉する仕切板、上記燃
料ダクト内と酸化ガス流通路内にそれぞれ設けられた燃
料ガス圧力検出器と酸化ガス圧力検出器、同それぞれの
圧力検出器より圧力信号を入力し制御信号を出力する駆
動制御装置、および同制御装置より制御信号を入力して
上記仕切板を駆動する仕切板駆動装置を具備したことを
特徴としている。
[Means for Solving the Problems] In the power generation device equipped with the differential pressure adjustment device of the present invention, the fuel duct and the oxidizing gas flow passage are connected to the residual fuel gas duct, and the voltage generation part support frame and the interconnector are used for sealing. In a power generation device equipped with fuel cells stacked through gaskets, a partition plate provided in the residual fuel gas duct to open and close the duct, and a fuel gas pressure detection device provided in the fuel duct and the oxidizing gas flow path, respectively. a drive control device that inputs pressure signals from the respective pressure detectors and outputs control signals, and a partition plate drive device that inputs control signals from the control device to drive the partition plate. It is characterized by having the following.

【0021】[0021]

【作用】上記において、燃料ガス圧力検出器と酸化ガス
圧力検出器はそれぞれ燃料ダクト内と酸化ガス流通路内
の圧力を検出して圧力信号を出力する。上記圧力信号は
駆動制御装置に入力され、同制御装置は上記燃料ダクト
内と酸化ガス流通路内の圧力が等しくなるように仕切板
駆動装置を介して仕切板を駆動し、仕切板の位置を調節
する。
[Operation] In the above, the fuel gas pressure detector and the oxidant gas pressure detector detect the pressure in the fuel duct and the oxidant gas flow path, respectively, and output pressure signals. The pressure signal is input to the drive control device, and the control device drives the partition plate via the partition plate drive device so that the pressure in the fuel duct and the oxidant gas flow path are equal, and determines the position of the partition plate. Adjust.

【0022】この調節により燃料ガスの圧力は上昇し、
酸化ガスの圧力とほゞ等しくなるため、燃料電池に設け
られたシール用ガスケットを介して燃料ダクトへの酸化
ガスの漏洩は抑制される。
[0022] Due to this adjustment, the pressure of the fuel gas increases,
Since the pressure is approximately equal to the pressure of the oxidizing gas, leakage of the oxidizing gas to the fuel duct via the sealing gasket provided in the fuel cell is suppressed.

【0023】上記により、燃料ダクト内の燃料ガスの圧
力を酸化ガス流通路の圧力に見合った圧力まで上昇させ
ることが可能となったため、燃料電池のシール用ガスケ
ットからの酸化ガスの漏洩を抑制することが可能となる
[0023] As a result of the above, it has become possible to increase the pressure of the fuel gas in the fuel duct to a pressure commensurate with the pressure in the oxidant gas flow path, thereby suppressing leakage of oxidant gas from the sealing gasket of the fuel cell. becomes possible.

【0024】[0024]

【実施例】本発明の一実施例を図1及び図2により説明
する。なお、本実施例においては、差圧調整装置の部分
以外は従来の技術の欄に記載した先願に係る装置と変ら
ないため、その説明を省略する。
[Embodiment] An embodiment of the present invention will be explained with reference to FIGS. 1 and 2. In addition, in this embodiment, since the parts other than the differential pressure adjusting device are the same as the device according to the prior application described in the section of the prior art, the explanation thereof will be omitted.

【0025】図1及び図2に示す本実施例は、先端にア
フタバーナ16を有する残存燃料ガスダクト52を中央
部に有する板状耐火部材32dにより排ガス室31と燃
料電池収納室35が左右に分割され、図3及び図4に示
すように電圧発生部支持枠10とインタコネクタ11が
シール用ガスケット8を介して積層され同支持枠10と
インタコネクタ11の間に燃料ガス通路2と酸素ガス通
路7が形成された複数の燃料電池9が、上記燃料電池収
納室35内の燃料ダクト12内に配設され、酸化ガス流
通路41aを有するシールガスケット用重し20が上記
燃料電池9の上面に設けられた発電装置において、上記
板状耐火部材32dに設けられその上部より燃料ダクト
12まで貫通する案内溝内にシリンダとピストンが設け
られ上部に駆動部を有する仕切板駆動装置53、同駆動
装置53のピストンの下端に設けられた仕切板51、上
記燃料ダクト12内に配設された燃料ガス圧力検出器5
5、上記シールガスケット用重し20に設けられた酸化
ガス流通路41a内に配設された酸化ガス圧力検出器5
6、および上記燃料ガス圧力検出器55と酸化ガス圧力
検出器56が電線により接続され上記仕切板駆動装置5
3を制御する駆動制御装置54を備えている。
In the present embodiment shown in FIGS. 1 and 2, an exhaust gas chamber 31 and a fuel cell storage chamber 35 are divided into left and right sides by a plate-shaped fireproof member 32d having a residual fuel gas duct 52 in the center having an afterburner 16 at its tip. , as shown in FIGS. 3 and 4, a voltage generator support frame 10 and an interconnector 11 are stacked with a sealing gasket 8 in between, and a fuel gas passage 2 and an oxygen gas passage 7 are provided between the support frame 10 and the interconnector 11. A plurality of fuel cells 9 in which a plurality of fuel cells 9 are formed are arranged in the fuel duct 12 in the fuel cell storage chamber 35, and a seal gasket weight 20 having an oxidizing gas flow passage 41a is provided on the upper surface of the fuel cell 9. In the power generation device, a cylinder and a piston are provided in a guide groove provided in the plate-shaped fireproof member 32d and penetrating from the upper part to the fuel duct 12, and a partition plate drive device 53 having a drive section in the upper part; a partition plate 51 provided at the lower end of the piston; a fuel gas pressure detector 5 provided within the fuel duct 12;
5. Oxidizing gas pressure detector 5 disposed within the oxidizing gas flow passage 41a provided in the seal gasket weight 20
6, and the partition plate driving device 5 in which the fuel gas pressure detector 55 and the oxidizing gas pressure detector 56 are connected by an electric wire.
A drive control device 54 is provided to control the motor.

【0026】上記において、酸化ガス流通路41a内に
配設された燃料ガス圧力検出器55と燃料ダクト12内
に配設された酸化ガス圧力検出器56がそれぞれ出力し
た検出信号は駆動制御装置54に入力され、同駆動制御
装置54は液圧を切換弁を介して前記仕切弁駆動装置5
3に送る。
In the above, the detection signals outputted by the fuel gas pressure detector 55 disposed in the oxidizing gas flow path 41a and the oxidizing gas pressure detector 56 disposed in the fuel duct 12 are sent to the drive control device 54. The drive control device 54 inputs the hydraulic pressure to the gate valve drive device 5 via the switching valve.
Send to 3.

【0027】前記残存燃料ガスダクト52を開閉する仕
切板51を駆動する仕切弁駆動装置53は、燃料ガス圧
力検出器55の圧力が酸化ガス圧力検出器56の圧力に
等しくなるように仕切板51の位置を調節し、燃料電池
9のシール用ガスケット8からの酸化ガス4の燃料ダク
ト12(または燃料電池収納室4)への漏洩を極少とす
る。
The gate valve driving device 53 that drives the partition plate 51 that opens and closes the residual fuel gas duct 52 controls the partition plate 51 so that the pressure of the fuel gas pressure detector 55 is equal to the pressure of the oxidizing gas pressure detector 56. The position is adjusted to minimize leakage of oxidizing gas 4 from sealing gasket 8 of fuel cell 9 into fuel duct 12 (or fuel cell storage chamber 4).

【0028】上記により、燃料ダクト内の燃料ガスの圧
力を酸化ガス流通路の圧力に見合った圧力まで上昇させ
ることを可能としたため、燃料電池のシール用ガスケッ
トからの酸化ガスの漏洩を抑制することが可能となった
[0028] As a result of the above, it is possible to increase the pressure of the fuel gas in the fuel duct to a pressure commensurate with the pressure in the oxidant gas flow path, thereby suppressing the leakage of oxidant gas from the sealing gasket of the fuel cell. became possible.

【0029】[0029]

【発明の効果】本発明の差圧調整装置を備えた発電装置
は、燃料ガス圧力検出器と酸化ガス圧力検出器がそれぞ
れ燃料ダクト内と酸化ガス流通路内の圧力を検出してそ
れぞれの圧力信号を駆動制御装置へ入力し、同制御装置
が仕切板駆動装置を介して残存燃料ダクトに設けられた
仕切板の位置を調節することによって、燃料ダクト内の
燃料ガスの圧力を酸化ガス流通路の圧力に見合った圧力
まで上昇させることが可能となったため、燃料電池のシ
ール用ガスケットからの酸化ガスの漏洩を抑制すること
が可能となる。
Effects of the Invention In the power generation device equipped with the differential pressure adjustment device of the present invention, the fuel gas pressure detector and the oxidant gas pressure detector detect the pressures in the fuel duct and the oxidant gas flow path, respectively, and adjust the pressure accordingly. A signal is input to the drive control device, and the control device adjusts the position of the partition plate provided in the remaining fuel duct via the partition plate drive device, thereby adjusting the pressure of the fuel gas in the fuel duct to the oxidizing gas flow path. Since it is now possible to increase the pressure to a value commensurate with the pressure of the fuel cell, it becomes possible to suppress leakage of oxidizing gas from the sealing gasket of the fuel cell.

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

【図1】本発明の一実施例に係る発電装置の説明図であ
る。
FIG. 1 is an explanatory diagram of a power generation device according to an embodiment of the present invention.

【図2】図1のA−A矢視図である。FIG. 2 is a view taken along the line A-A in FIG. 1;

【図3】平板型固体電解質燃料電池の斜視図である。FIG. 3 is a perspective view of a flat plate solid electrolyte fuel cell.

【図4】図3のB−B矢視図である。FIG. 4 is a view taken along the line BB in FIG. 3;

【図5】先願に係る発電装置の説明図である。FIG. 5 is an explanatory diagram of a power generation device according to a prior application.

【符号の説明】[Explanation of symbols]

1        燃料ガス 4        酸化ガス 8        シール用ガスケット9      
  燃料電池 10      電圧発生部支持枠 11      インタコネクタ 12      燃料ダクト 15      残存燃料ガス 16      アフタバーナ 31      排ガス室 32d    板状耐火部材 35      燃料電池収納室 51      仕切板 52      残存燃料ガスダクト 53      仕切板駆動装置 54      駆動制御装置 55      燃料ガス圧力検出器 56      酸化ガス圧力検出器
1 Fuel gas 4 Oxidizing gas 8 Seal gasket 9
Fuel cell 10 Voltage generator support frame 11 Interconnector 12 Fuel duct 15 Residual fuel gas 16 Afterburner 31 Exhaust gas chamber 32d Plate fireproof member 35 Fuel cell storage chamber 51 Partition plate 52 Residual fuel gas duct 53 Partition plate drive device 54 Drive control device 55 Fuel gas pressure detector 56 Oxidizing gas pressure detector

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  燃料ダクトと酸化ガス流通路が接続さ
れ残存燃料ガスダクトに接続され電圧発生部支持枠とイ
ンタコネクタがシール用ガスケットを介して積層された
燃料電池を備えた発電装置において、上記残存燃料ガス
ダクトに設けられ同ダクトを開閉する仕切板、上記燃料
ダクト内と酸化ガス流通路内にそれぞれ設けられた燃料
ガス圧力検出器と酸化ガス圧力検出器、同それぞれの圧
力検出器より圧力信号を入力し制御信号を出力する駆動
制御装置、および同制御装置より制御信号を入力して上
記仕切板を駆動する仕切板駆動装置を具備したことを特
徴とする差圧調整装置を備えた発電装置。
Claim 1. A power generation device comprising a fuel cell in which a fuel duct and an oxidizing gas flow passage are connected to a residual fuel gas duct, and a voltage generating part support frame and an interconnector are stacked via a sealing gasket. A partition plate installed in the fuel gas duct to open and close the duct, a fuel gas pressure detector and an oxidant gas pressure detector installed in the fuel duct and the oxidant gas flow path, respectively, and a pressure signal is received from each pressure detector. What is claimed is: 1. A power generation device equipped with a differential pressure adjustment device, comprising: a drive control device that inputs a control signal and outputs a control signal; and a partition plate drive device that inputs a control signal from the control device and drives the partition plate.
JP3095246A 1991-04-25 1991-04-25 Generating unit provided with differential pressure adjusting device Withdrawn JPH04324254A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3095246A JPH04324254A (en) 1991-04-25 1991-04-25 Generating unit provided with differential pressure adjusting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3095246A JPH04324254A (en) 1991-04-25 1991-04-25 Generating unit provided with differential pressure adjusting device

Publications (1)

Publication Number Publication Date
JPH04324254A true JPH04324254A (en) 1992-11-13

Family

ID=14132400

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3095246A Withdrawn JPH04324254A (en) 1991-04-25 1991-04-25 Generating unit provided with differential pressure adjusting device

Country Status (1)

Country Link
JP (1) JPH04324254A (en)

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