JPH01286260A - Protecting device for fuel cell - Google Patents

Protecting device for fuel cell

Info

Publication number
JPH01286260A
JPH01286260A JP63116198A JP11619888A JPH01286260A JP H01286260 A JPH01286260 A JP H01286260A JP 63116198 A JP63116198 A JP 63116198A JP 11619888 A JP11619888 A JP 11619888A JP H01286260 A JPH01286260 A JP H01286260A
Authority
JP
Japan
Prior art keywords
gas
concentration
signal
fuel cell
stage
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP63116198A
Other languages
Japanese (ja)
Inventor
Heishiro Goto
後藤 平四郎
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji 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
Priority to JP11558688A priority Critical patent/JPS6451994A/en
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP63116198A priority patent/JPH01286260A/en
Publication of JPH01286260A publication Critical patent/JPH01286260A/en
Pending 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
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/247Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
    • 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

PURPOSE:To perform the stable long-term power generation operation by providing multi-stage comparators in a judging circuit and performing the control in response to the leaked combustible gas concentration. CONSTITUTION:When fuel gas 9 is leaked in a cell, the light combustible gas is floated in a frame 2 and collected from the frame 2 into a collecting chamber 21 protruded upward. When the combustible gas concentration in the collecting chamber 21 is increased, the level of the concentration actual signal 6A of a detector 6 is increased. The signal 6A is compared with set values of the corresponding first-stage comparator 22, second-stage comparator 23, and highest-level comparator 24 by a judging circuit 20, control signals 22C-24C are issued when they are higher than the set values. The signal 22C opens a solenoid valve 27B and releases the mixed gas 31 from a releasing mechanism section 27, the signal 23C releases the gas 31 from a releasing mechanism section 28. The signal 24C controls and operates an abnormality control circuit 25 and issues an alarm 25A and stops the operation. The situation is coped with in stages, the operation is not stopped when the level of the signal 6A is lowered at the low stage, thereby the stable long-term operation can be performed.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、燃料電池積層体が筐体内に所定圧力の不活
性ガスとともに収納された燃料電池の筐体内に漏れた可
燃性ガス濃度を所定濃度以下に抑妊える保護装置に関す
る。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is directed to controlling the concentration of combustible gas leaked into the casing of a fuel cell in which a fuel cell stack is housed together with an inert gas at a predetermined pressure in the casing. It relates to a protective device that suppresses the concentration below.

〔従来の技術〕[Conventional technology]

第2図は従来装置を示す燃料電池の概略断面図であシ、
多数の単電池を積層しその積層面に所定の面圧が加えら
れてなる燃料電池積層体(以下スタックと呼ぶ21は筐
体2内に支持され、その互いに対向する側面には例えば
複数ブロックに分割された燃料ガス9の給排マニホール
ド6Aおよび3Bが気密に取付けられ、供給側集合配管
4Aおよび排出側果合配管4Bによ〕筐体2の外部に引
き出される。また、スタック1の他の二つの側面には図
示しない酸化剤としての反応空気の給排マニホールドお
よび給排集合配管が気密に連結され筐体2の外部に引き
出される。また、筐体2には不活性ガスとしての例えば
窒素(Nz)10の供給管5Aが設けられ筐体2の底部
に近い位置に開口した供給管5Aから筐体内に所定の圧
力のN2が供給される。また5Bは筐体2の上部に開口
部を有する窒素排出管であシ、その出口側には例えばd
」変絞ジ弁7が設けられ、各独ガス圧の変化に対応して
少量の不活性ガスが筐体から排出されることKよシ、燃
料ガス、反応空気、および不活性ガス相互の圧力バラン
スが保持されて発電運転が行われる。
FIG. 2 is a schematic cross-sectional view of a fuel cell showing a conventional device.
A fuel cell stack 21 (hereinafter referred to as a stack), which is formed by stacking a large number of single cells and applying a predetermined surface pressure to the stacked surfaces, is supported in the casing 2, and the mutually opposing sides thereof are provided with a plurality of blocks, for example. The divided supply/discharge manifolds 6A and 3B of the fuel gas 9 are airtightly attached, and are drawn out of the housing 2 by the supply side collection pipe 4A and the discharge side output pipe 4B. A supply/discharge manifold and a supply/discharge collection pipe for reaction air as an oxidizing agent (not shown) are airtightly connected to the two sides and drawn out to the outside of the housing 2.In addition, the housing 2 is equipped with an inert gas such as nitrogen. (Nz) 10 supply pipes 5A are provided, and N2 at a predetermined pressure is supplied into the housing from the supply pipes 5A that open near the bottom of the housing 2. Also, 5B has an opening at the top of the housing 2. It is a nitrogen exhaust pipe with a
A variable throttle valve 7 is provided to allow a small amount of inert gas to be discharged from the housing in response to changes in the respective gas pressures, and to control the mutual pressure of the fuel gas, reaction air, and inert gas. The balance is maintained and power generation operation is performed.

ところで、燃料ガスおよび反応空気はその差圧を所定レ
ベル以下に抑さえた状態で燃料電池の作動温度を保持し
て発電運転が行われるが、筐体2に収納された燃料電池
中床にはスタック1とマニホールドとの接合部やマニホ
ールドと集合管の接合部など多くの接合部を持ち、これ
ら接合部のシール面から筐体2内に燃料ガスや反応空気
が漏れる可能性がある。そこで、筐体内の不活性ガス1
0のガス圧を燃料ガスおよび反応空気のガス圧よシ10
0ないし300 mmAq al&常に高く保持するこ
とにより、燃料ガスまたは反応空気が筐体2内に漏れな
いよう構成される。
By the way, power generation operation is carried out by maintaining the operating temperature of the fuel cell with the differential pressure of the fuel gas and reaction air suppressed below a predetermined level. It has many joints, such as the joint between the stack 1 and the manifold, and the joint between the manifold and the collecting pipe, and there is a possibility that fuel gas or reaction air may leak into the casing 2 from the sealing surfaces of these joints. Therefore, inert gas 1 inside the housing
0 gas pressure to the gas pressure of fuel gas and reaction air 10
0 to 300 mmAq al& By keeping it always high, the fuel gas or reaction air is configured to prevent leakage into the housing 2.

しかしながら、不測のガス漏れに備えて不活性ガスの排
出管5BKVi可燃性ガス濃度の検知センサ6が設けら
れ、筐体2内に漏れた水素(H2)。
However, in preparation for an unexpected gas leak, an inert gas exhaust pipe 5BKVi and a combustible gas concentration detection sensor 6 are provided to detect hydrogen (H2) leaking into the housing 2.

メタン(CH4)、−酸化炭素(CO)等の比重が不活
性ガスとしての窒素に比べて軽いために、筐体2の上部
に漏えいol燃性ガス溜り11を形成することを利用し
、可燃性ガス溜り11近傍に入口が開口した排出W5B
を介して不燃性ガスとともに排出される可燃性ガスの濃
度を検知センサ6で検出し、出力信号レベルが所定レベ
ルを超えたとき誉報を発する制御回路8により、例えば
燃料電池の発電運転を非常停止させる保護装置を備えた
ものが知られている。
Since the specific gravity of methane (CH4), -carbon oxide (CO), etc. is lighter than that of nitrogen as an inert gas, the formation of a leakage ol flammable gas reservoir 11 in the upper part of the housing 2 is utilized. Exhaust W5B with an inlet near the gas reservoir 11
A detection sensor 6 detects the concentration of combustible gas discharged together with nonflammable gas through a control circuit 8 that issues an alarm when the output signal level exceeds a predetermined level. Some devices are known that are equipped with a protection device to stop them.

〔発明が解決しようとする諌租〕[The problem that the invention aims to solve]

前述の燃料電池の発電運転中に電気的負荷の急増急減や
非常停止などがあると、燃料電池の燃料または反応空気
の消費量と供給量とのタイミングのずれに基づいてガス
圧が変化する。ことに、負荷の急減時や非常停止時には
消費ガス量の急減によってガス圧が上昇し、この上昇し
たガス圧が過渡的に不活性ガス圧に近接または超えるこ
とによって燃料ガスおよび反応空気の漏れが急増する事
態が発生することがある。このような事態の発生は、i
」燃性ガス溜りへの可燃性ガス量の滞留量を増加させる
とともに、不活性ガス中の酸素濃度を高め、jilil
ガスの混触によるガス爆発の危険性を高める。しかしな
がら、従来技術のように少量の不活性ガスを流す方法で
は多iK漏れた可燃性ガスを排出するのに時間がかかり
、その結果燃料電池の発電運転を非常停止する頻度が高
まり燃料電池の長時間発電運転が阻害されるという問題
がある。
If there is a sudden increase or decrease in electrical load or an emergency stop during the above-described power generation operation of the fuel cell, the gas pressure will change based on the timing difference between the amount of fuel or reaction air consumed by the fuel cell and the amount of supply. In particular, when the load suddenly decreases or there is an emergency stop, the gas pressure increases due to the sudden decrease in the amount of gas consumed, and this increased gas pressure transiently approaches or exceeds the inert gas pressure, causing leakage of fuel gas and reaction air. A sudden increase may occur. The occurrence of such a situation is i
"Increases the amount of combustible gas retained in the flammable gas reservoir, increases the oxygen concentration in the inert gas, and
Increases the risk of gas explosion due to gas mixture. However, with the conventional method of flowing a small amount of inert gas, it takes a long time to exhaust the leaked flammable gas, which increases the frequency of emergency stop of the fuel cell's power generation operation and increases the length of the fuel cell. There is a problem that hourly power generation operation is inhibited.

この発明の目的は、筐体内に漏れた可燃性ガスをその漏
れ量に対応して早期に排出できるとともに、危険なレベ
ルの漏れ量が生じたときはじめて非常停止信号を出すこ
とにより長期発電運転を安定化させることにある。
The purpose of this invention is to quickly discharge flammable gas that has leaked into the housing according to the amount of leakage, and to maintain long-term power generation operation by issuing an emergency stop signal only when a dangerous level of leakage occurs. The goal is to stabilize it.

〔諌顕を解決するための手段〕[Means to resolve the problem]

上記課題を解決するために、この発明によれば。 According to the present invention, the above problems can be solved.

燃料電池積層体と、この燃料電池積層体に燃料ガスおよ
び酸化剤ガスをそれぞれ給排出する反応ガス通路とを含
む燃料電池中味が所定圧力の不活性ガスの給排通路を有
する筐体内に収納されたものにおいて、前記筐体の上方
に凸に形成された漏えい可燃性ガスの捕集室と、この捕
集室に設けられた可燃性ガス濃度の検知器と、この検知
器の検出濃度実際値信号を複数段階の設定値信号と比較
して濃度段階別の制御信号を発する判断回路と、前記捕
集室に連結された放出ガス流量の制御弁からなり前記制
御信号により制御されて濃度段1s![相応した流量の
可燃性ガスを不活性ガスとともに放出する放出機構部と
、最高濃度段階の制御信号を受けて非常停止を指令する
信号を発する異常制御回路とを備えるものとする。
The contents of the fuel cell, including a fuel cell stack and a reaction gas passage for supplying and discharging fuel gas and oxidizing gas to and from the fuel cell stack, respectively, are housed in a casing having a supply and discharge passage for inert gas at a predetermined pressure. A collection chamber for leaking combustible gas formed in a convex manner above the housing, a detector for the concentration of the combustible gas provided in the collection chamber, and an actual value of the concentration detected by the detector. It consists of a judgment circuit that compares the signal with set value signals of multiple stages and issues a control signal for each concentration stage, and a control valve for the flow rate of released gas connected to the collection chamber, and is controlled by the control signal to generate a concentration stage 1s. ! [It shall be equipped with a discharge mechanism section that discharges a corresponding flow rate of flammable gas together with an inert gas, and an abnormality control circuit that receives a control signal at the highest concentration stage and issues a signal instructing an emergency stop.]

〔作用〕[Effect]

上記手段において、筐体の上方に可燃性ガスの捕集室を
突設して可燃性ガス濃度の検知器を設けたことKより、
筐体内に漏れた可燃性ガスの捕集および濃度検知が迅速
化される。また判断回路を設けて検知器の検出濃度実際
値信号を複数段階の設定値信号と比較して濃度段階別の
制御信号を出力させ、この制御信号により制御弁からな
る放出機構部の放出ガス流!−を検出ガス濃度に対応し
て制御することにより、例えば可燃性ガスの小量の漏れ
は初段の制御信号によって小さな放出流量で放出が行な
われることにより不活性ガス圧に影響を及ぼすことなく
排出でき、漏れ量がさらに大きい場合には捕集室の可燃
性ガス濃度が上昇するので、次段の1トリ御信号によっ
て放出ガス量が増し可燃性ガスの放出が迅速化される。
In the above means, since the flammable gas collection chamber is protruded above the housing and the flammable gas concentration detector is provided,
Collecting and detecting the concentration of flammable gas leaking into the housing is accelerated. In addition, a judgment circuit is provided to compare the actual concentration value signal detected by the detector with the set value signals of multiple stages and output a control signal for each concentration stage. ! - By controlling the gas concentration according to the detected gas concentration, for example, if a small amount of combustible gas leaks, the first stage control signal allows the gas to be released at a small flow rate, without affecting the inert gas pressure. If the amount of leakage is larger, the concentration of flammable gas in the collection chamber increases, so the amount of gas released is increased by the next-stage one-trick control signal, and the release of combustible gas is accelerated.

漏れ量が更に大きく摘果室の可燃性ガス濃度が危険領域
に達すると最高a度段階の制御信号が出力され、異常制
御回路から蕾報信号2発電運転の非常停止指令信号が出
力されることにより、装置が保論されるとともに、危険
な漏れ址に到達したときにのみ非常停止信号が出力され
るので長期発電運転に及ぼす影響を最小限に抑さえた保
護を行うことができる。
When the amount of leakage becomes larger and the concentration of combustible gas in the fruit picking room reaches the dangerous range, a control signal of the highest level A is output, and an emergency stop command signal for bud alarm signal 2 power generation operation is output from the abnormality control circuit. Since the system is protected, and an emergency stop signal is output only when a dangerous leakage point is reached, protection can be achieved with minimal impact on long-term power generation operation.

〔実施例〕〔Example〕

以下この発明を実施例に基づいて説明する。 The present invention will be explained below based on examples.

第1図はこの発明の実施例装置を示す構成図であり、従
来装置と共通する部分には同一参照符号を用いることに
よジ詳細な!52明を省略する。図において、筐体2の
上部にはその蓋板2Aに下端カ開口した管状の捕集室2
1が突設され、摘果室21には固定絞D27Aおよび電
磁弁27Bの直列体からなる初段の放出機構部27と、
例えば電動制御弁等の次段の放出機構部28とで構成さ
れる放出機構部26が設けられ、それぞれの吐出側が排
気管29に連通ずるよう形成される。可燃性ガス濃度の
検知器としての例えば水素ガス濃度センサ6は摘果室2
1に取付けられ、その出力信号としての濃度実際値信号
6Aは判断回路20に向けて出力される。
FIG. 1 is a block diagram showing a device according to an embodiment of the present invention, and the same reference numerals are used for parts common to the conventional device for detailed explanation. 52 omitted. In the figure, the upper part of the housing 2 has a tubular collection chamber 2 whose lower end is opened on the lid plate 2A.
1 is provided protrudingly, and in the fruit-thinning chamber 21, there is a first-stage release mechanism section 27 consisting of a series body of a fixed diaphragm D27A and a solenoid valve 27B;
For example, a discharge mechanism section 26 composed of a next-stage discharge mechanism section 28 such as an electric control valve is provided, and each discharge side is formed to communicate with an exhaust pipe 29 . For example, a hydrogen gas concentration sensor 6 as a detector for combustible gas concentration is located in the fruit picking chamber 2.
1, and its output signal, the actual concentration value signal 6A, is outputted to the judgment circuit 20.

判断回路20は初段比較器222次段比較器23、最高
レベルの比較器24など複数の比較器を持ち、濃度実際
値信号6Aはそれぞれの比較器に入力され、設定器22
A、23A、24Aの濃度段階別設定信号228.23
S、243とそれぞれ比較され、初段比較器の出力制御
信号22Cによって初段の放出機構部27の電磁弁27
Bが開閉制御され、次段比較器26の出力制御信号23
Cによって次段の放出機構部28の放出流を力;緩やか
に増丁よう制御される。筐た、最高レベルの比較器24
の出力制御信号24Cは異常flflJ御回路25に入
力ちれ、実際値信号6Aが最高レベルの設定11II2
4Sのレベルを超えたとき、誉報信号25Aおよび発電
運転の非常停止指令信号25Bが出力される。
The judgment circuit 20 has a plurality of comparators such as a first stage comparator 222, a second stage comparator 23, and a highest level comparator 24, and the actual concentration value signal 6A is input to each comparator, and the setter 22
A, 23A, 24A concentration level setting signal 228.23
The electromagnetic valve 27 of the first stage discharge mechanism section 27 is compared with the first stage comparator output control signal 22C.
B is controlled to open and close, and the output control signal 23 of the next stage comparator 26
C controls the ejection flow of the next stage ejection mechanism section 28 so as to gradually increase the number of copies. The highest level comparator 24
The output control signal 24C is input to the abnormal flflJ control circuit 25, and the actual value signal 6A is set to the highest level 11II2.
When the level of 4S is exceeded, an honor signal 25A and an emergency stop command signal 25B for power generation operation are output.

上述のように構成された実施例装置の発電運転中に燃料
電池のスタック1.マニホールド3A。
During power generation operation of the embodiment device configured as described above, the fuel cell stack 1. Manifold 3A.

3B、果合配管4A 、4B等からなる燃料電池中身で
燃料ガス9の漏れが発生すると、不活性ガスとしての窒
素10に比べて軽い水素、炭化水素。
When fuel gas 9 leaks from inside the fuel cell, which consists of pipes 3B, 4A, 4B, etc., hydrogen and hydrocarbons, which are lighter than nitrogen 10 as an inert gas, leak.

−酸化炭素などの可燃性ガスは筐体2内を浮上して一体
2の上方に突設された捕集室21に集まり、不活性ガス
と可燃性ガスとの混合ガス31中の可燃性ガス濃度が高
まり、例えば水素濃度の検知器6が出力する濃度実際値
信号6Aのレベルが上昇するので、判断回路20で設定
値と比較することにより制御信号が出力される。
- Combustible gas such as carbon oxide floats inside the housing 2 and collects in the collection chamber 21 protruding above the unit 2, and the combustible gas in the mixed gas 31 of inert gas and combustible gas As the concentration increases, for example, the level of the actual concentration signal 6A output from the hydrogen concentration detector 6 increases, so the determination circuit 20 compares it with a set value and outputs a control signal.

複数濃度段階の設定値としては、可燃性ガスの爆発限界
(下限値ン以下とすることが好ましく、例えば初段設定
値22Sとして5QQPPm、次段設定値23Sとして
1.000PPm、最高レヘルノ設定(If 24 S
として3000PPmO!うに爆発限界の1/10以下
に選ぶことができる。
The setting values for multiple concentration stages are preferably below the explosion limit (lower limit) of combustible gas; for example, the first stage setting value 22S is 5QQPPm, the second stage setting value 23S is 1.000PPm, and the highest level setting (If 24 S
As 3000PPmO! Sea urchin can be selected to be less than 1/10 of the explosive limit.

判断回路20の各比較器22,23,24の設定濃度レ
ベルを上述のように多段階に設定したと仮定すると、摘
果室21内の水素濃度が500PP m VC到達した
時点で初段比較器22から制御信号22Cが出力されて
初段の放出機構部27の電磁弁27Bが開き、固定絞り
27Aによって放出ガス流量が絞られた混合ガス31が
排出される。
Assuming that the concentration levels of the comparators 22, 23, and 24 of the judgment circuit 20 are set in multiple stages as described above, when the hydrogen concentration in the fruit thinning chamber 21 reaches 500 PP m VC, the first stage comparator 22 When the control signal 22C is output, the electromagnetic valve 27B of the first-stage discharge mechanism section 27 opens, and the mixed gas 31 whose discharge gas flow rate has been throttled by the fixed throttle 27A is discharged.

この初段の放出によって捕集室21の混合ガス中の水素
濃度が低下してしまうようであれば、可燃性ガスの漏れ
による爆発の危険性はないので、放出を間欠的に繰り返
しつつ発電運転が続けられ、ガス放出による不活性ガス
10の圧力低下は供給管5Aからの補給不活性ガスによ
り桶償される。
If the hydrogen concentration in the mixed gas in the collection chamber 21 decreases due to this first-stage release, there is no danger of explosion due to leakage of flammable gas, so power generation operation can be continued while repeating the release intermittently. The pressure drop in the inert gas 10 due to the gas discharge is compensated by the supplementary inert gas from the supply pipe 5A.

摘果室21の水素ガス濃度がさらに上昇するようであれ
ば、水素ガス濃度が11000PPに到達した時点で次
段比奴器23から制御信号23Cが出力されて電動弁2
8が徐々に開き、初段および次段の放出機構部27.2
8の双方から混合ガス31が放出される。なお、次段の
放出機構部28を電動弁として徐々に放出ガス量を増す
よう構成した理由は、放出ガス量を急増させることくよ
って筐体内の不活性ガス圧が下がり、燃料ガス系。
If the hydrogen gas concentration in the fruit-picking chamber 21 rises further, the control signal 23C is output from the next-stage rice cooker 23 when the hydrogen gas concentration reaches 11,000 PP, and the electric valve 2
8 gradually opens, and the first stage and next stage release mechanism parts 27.2
Mixed gas 31 is released from both sides of 8. The reason why the discharge mechanism section 28 in the next stage is configured as an electric valve to gradually increase the amount of released gas is that by rapidly increasing the amount of released gas, the inert gas pressure inside the housing decreases, and the fuel gas system.

反応孕気糸のガス圧に対する差圧が縮まることによって
燃料ガス9の漏れ:itを増大させる原因を作ることを
避けるためであり、放出ガス量の増大速度は不活性ガス
10の供給増加速度に基づいて決められる。このように
2段階の放出ガス量の制御によって捕集室21の水素ガ
ス濃度が低下するようであれば、また発電運転可能と判
断されて運転が持続される。
This is to avoid causing an increase in leakage of fuel gas 9 due to a reduction in the differential pressure with respect to the gas pressure of the reaction-containing air, and the rate of increase in the amount of released gas is equal to the rate of increase in the supply of inert gas 10. determined based on. If the hydrogen gas concentration in the collection chamber 21 decreases by controlling the amount of released gas in two stages as described above, it is determined that power generation operation is possible again, and operation is continued.

捕集室21の水素ガス濃度が更に上昇し300QPPm
に到達すると、最高レベルの比較器24から制御信号2
4Sが出力され、異常制御回路25が動作して誉報25
A、非常停止指令信号25B等が出力されることにより
、燃料電池への燃料ガスの供給や停止や燃料ガス禾9反
応伊気糸などの不活性ガスによるパージなど非常停止に
必要な操作が行われるとともに、検知器6がol燃性ガ
ス濃度の低下を検知して弁28.27Bの順に放出機構
部26のガス放出を停止させることにより、燃料電池の
保膣動作が完了する。
The hydrogen gas concentration in the collection chamber 21 further increases to 300QPPm.
, the control signal 2 is output from the highest level comparator 24.
4S is output, the abnormality control circuit 25 operates, and the honor signal 25 is output.
A. By outputting the emergency stop command signal 25B, etc., operations necessary for an emergency stop can be performed, such as supplying or stopping fuel gas to the fuel cell, or purging with an inert gas such as fuel gas. At the same time, the detector 6 detects a decrease in the concentration of the ol combustible gas, and the valves 28, 27B, in turn, stop the gas discharge from the discharge mechanism section 26, thereby completing the maintenance operation of the fuel cell.

〔発明の効果〕〔Effect of the invention〕

この発明は前述のように、燃料電池中身を所定圧力の不
活性ガスとともに収蔵する筐体の上方に漏えい可燃性ガ
スの捕集室を突設して可燃性ガス濃度の検知器を設け、
その出力実際値信号を複数濃度段階の設定値と比較して
それぞれ制御信号を出力する判断部により、放出ガス量
が濃度段階に対応して段階的に異なる放出機構部および
異常制御回路を制御するよう構成した。その結果、燃料
電池中味から漏れた軽いb]燃性ガスは重い不活性ガス
中を浮上して捕集室内の可燃性ガス濃度を高め、これを
検知した検知器および判断部が、濃度段階に応じて放出
機構部の放出ガス量を段階的に制御するので、燃料ガス
の漏洩規模に対応した放出ガス菫の制御が可能となり、
小規模のガス漏れに対しては筐体内の可燃性ガス濃度を
危険性のないレベルに抑さえて発電運転を安定して持続
することができる。また、放出機構部の放出ガス量では
捕集室内可燃性ガス濃度を下げられない規模のガス漏れ
が生じたときはじめて異常制御回路が警報および非常停
止指令信号を出力するので、燃料電池の危険状態を回避
できるとともに、従来装置に比べて危険状態が正確に把
握されるので、発電運転が度々非常停止されることによ
って長期発電運転が阻害されることのない燃料電池の保
護装置を提供することができる。
As described above, this invention provides a collection chamber for leaking flammable gas that protrudes above a housing that stores the contents of a fuel cell together with an inert gas at a predetermined pressure, and a detector for detecting the concentration of combustible gas.
A determination unit that compares the output actual value signal with set values for multiple concentration levels and outputs control signals respectively controls the release mechanism unit and the abnormality control circuit in which the amount of released gas varies in stages corresponding to the concentration level. It was configured as follows. As a result, the light flammable gas leaking from the fuel cell contents floats up in the heavy inert gas and increases the concentration of combustible gas in the collection chamber, and the detector and judgment unit that detects this increases the concentration level. Since the amount of gas released from the release mechanism is controlled in stages accordingly, it is possible to control the amount of released gas depending on the scale of the fuel gas leak.
In the case of small-scale gas leaks, the concentration of flammable gas within the housing can be suppressed to a non-hazardous level, allowing stable power generation operation to continue. In addition, the abnormality control circuit outputs an alarm and an emergency stop command signal only when a gas leak occurs on a scale that cannot reduce the combustible gas concentration in the collection chamber with the amount of gas released from the release mechanism, so the fuel cell is in a dangerous state. It is possible to provide a protection device for a fuel cell, which can avoid the danger and grasp dangerous conditions more accurately than conventional devices, so that long-term power generation operation is not hindered by frequent emergency stops of power generation operation. can.

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

第1図はこの発明の実施例装置を示す構成図、第2図は
従来装置を示す燃料電池の概略断面図である。 1・・・燃料電池積層体(スタック)、2・・・筐体、
6A 、3B・・・マニホールド(燃料ガス側)、4A
FIG. 1 is a block diagram showing a device according to an embodiment of the present invention, and FIG. 2 is a schematic sectional view of a fuel cell showing a conventional device. 1... fuel cell stack (stack), 2... casing,
6A, 3B... Manifold (fuel gas side), 4A
.

Claims (1)

【特許請求の範囲】[Claims] 1)燃料電池積層体と、この燃料電池積層体に燃料ガス
および酸化剤ガスをそれぞれ給排出する反応ガス通路と
を含む燃料電池中味が所定圧力の不活性ガスの給排通路
を有する筐体内に収納されたものにおいて、前記筐体の
上方に凸に形成された漏えい可燃性ガスの捕集室と、こ
の捕集室に設けられた可燃性ガス濃度の検知器と、この
検知器の検出濃度実際値信号を複数段階の設定値信号と
比較して濃度段階別の制御信号を発する判断回路と、前
記捕集室に連結された放出ガス流量の制御弁からなり前
記制御信号により制御されて濃度段階に相応した流量の
可燃性ガスを不活性ガスとともに放出する放出機構部と
、最高濃度段階の制御信号を受けて非常停止を指令する
信号を発する異常制御回路とを備えたことを特徴とする
燃料電池の保護装置。
1) The contents of the fuel cell, including a fuel cell stack and a reactive gas passage for supplying and discharging fuel gas and oxidizing gas to and from the fuel cell stack, respectively, are placed in a housing having a passage for supplying and discharging inert gas at a predetermined pressure. In the stored product, there is a collection chamber for leaking combustible gas formed in a convex manner above the housing, a detector for detecting the concentration of combustible gas provided in this collection chamber, and a detection concentration of the gas by the detector. It consists of a judgment circuit that compares the actual value signal with set value signals of multiple stages and issues a control signal for each concentration stage, and a control valve for controlling the flow rate of released gas connected to the collection chamber, and the concentration is controlled by the control signal. It is characterized by being equipped with a discharge mechanism section that releases flammable gas at a flow rate corresponding to the stage together with an inert gas, and an abnormality control circuit that receives a control signal for the highest concentration stage and issues a signal instructing an emergency stop. Fuel cell protection device.
JP63116198A 1988-05-12 1988-05-13 Protecting device for fuel cell Pending JPH01286260A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP11558688A JPS6451994A (en) 1988-05-12 1988-05-12 Album
JP63116198A JPH01286260A (en) 1988-05-13 1988-05-13 Protecting device for fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63116198A JPH01286260A (en) 1988-05-13 1988-05-13 Protecting device for fuel cell

Publications (1)

Publication Number Publication Date
JPH01286260A true JPH01286260A (en) 1989-11-17

Family

ID=14681264

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63116198A Pending JPH01286260A (en) 1988-05-12 1988-05-13 Protecting device for fuel cell

Country Status (1)

Country Link
JP (1) JPH01286260A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002367648A (en) * 2001-06-06 2002-12-20 Toyota Motor Corp Case for fuel cell
EP1408571A2 (en) * 2002-10-09 2004-04-14 Nissan Motor Co., Ltd. Container structure for fuel cell
JP2012017748A (en) * 2011-10-25 2012-01-26 Mitsubishi Heavy Ind Ltd Gas turbine device
JP2015038863A (en) * 2013-07-19 2015-02-26 日本特殊陶業株式会社 Fuel cell
US9097188B2 (en) 2008-10-01 2015-08-04 Mitsubishi Hitachi Power Systems, Ltd. Gas turbine device
JP6103120B1 (en) * 2016-02-12 2017-03-29 富士電機株式会社 FUEL CELL DEVICE AND FUEL CELL DEVICE OPERATION CONTROL METHOD

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59138075A (en) * 1983-01-26 1984-08-08 Hitachi Ltd Accommodation equipment of stack type fuel cell
JPS60177564A (en) * 1984-02-24 1985-09-11 Hitachi Ltd Fuel cell power generating system
JPS60208059A (en) * 1984-04-02 1985-10-19 Hitachi Ltd Protection device of fuel cell
JPS61147466A (en) * 1984-11-13 1986-07-05 Fuji Electric Co Ltd Supplying device for purge gas for fuel cell

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59138075A (en) * 1983-01-26 1984-08-08 Hitachi Ltd Accommodation equipment of stack type fuel cell
JPS60177564A (en) * 1984-02-24 1985-09-11 Hitachi Ltd Fuel cell power generating system
JPS60208059A (en) * 1984-04-02 1985-10-19 Hitachi Ltd Protection device of fuel cell
JPS61147466A (en) * 1984-11-13 1986-07-05 Fuji Electric Co Ltd Supplying device for purge gas for fuel cell

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002367648A (en) * 2001-06-06 2002-12-20 Toyota Motor Corp Case for fuel cell
EP1408571A2 (en) * 2002-10-09 2004-04-14 Nissan Motor Co., Ltd. Container structure for fuel cell
EP1408571A3 (en) * 2002-10-09 2005-09-21 Nissan Motor Co., Ltd. Container structure for fuel cell
US9097188B2 (en) 2008-10-01 2015-08-04 Mitsubishi Hitachi Power Systems, Ltd. Gas turbine device
JP2012017748A (en) * 2011-10-25 2012-01-26 Mitsubishi Heavy Ind Ltd Gas turbine device
JP2015038863A (en) * 2013-07-19 2015-02-26 日本特殊陶業株式会社 Fuel cell
JP6103120B1 (en) * 2016-02-12 2017-03-29 富士電機株式会社 FUEL CELL DEVICE AND FUEL CELL DEVICE OPERATION CONTROL METHOD
JP2017147215A (en) * 2016-02-12 2017-08-24 富士電機株式会社 Fuel cell device and method for controlling operation of fuel cell device

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