JPH07272739A - Fuel cell purge device - Google Patents

Fuel cell purge device

Info

Publication number
JPH07272739A
JPH07272739A JP6085734A JP8573494A JPH07272739A JP H07272739 A JPH07272739 A JP H07272739A JP 6085734 A JP6085734 A JP 6085734A JP 8573494 A JP8573494 A JP 8573494A JP H07272739 A JPH07272739 A JP H07272739A
Authority
JP
Japan
Prior art keywords
valve
cylinder
pressure
solenoid valve
fuel cell
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
JP6085734A
Other languages
Japanese (ja)
Other versions
JP3360766B2 (en
Inventor
Norihisa Kamiya
規寿 神家
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas 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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP08573494A priority Critical patent/JP3360766B2/en
Publication of JPH07272739A publication Critical patent/JPH07272739A/en
Application granted granted Critical
Publication of JP3360766B2 publication Critical patent/JP3360766B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • H01M8/04223Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
    • 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
    • H01M8/04223Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
    • H01M8/04228Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells during shut-down
    • 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
    • H01M8/2483Details of groupings of fuel cells characterised by internal manifolds
    • 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

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

Abstract

PURPOSE:To provide a device with no obstacle for protecting a catalyst, even when a power supply lost time is lengthened, by providing a fine flow valve or orifice in parallel to a primary pressure regulating valve in a cylinder collecting pipe in an inlet side of a pressure reducing valve. CONSTITUTION:A primary pressure adjusting valve 6 is interposed in a cylinder collecting pipe 2 in an inlet side of a pressure reducing valve 3, to provide a fine flow valve or orifice 7 in parallel to the valve 6. In a side of a fuel cell A, a current carrying closed type main solenoid valve 4 is interposed, to connect a catalyst protecting current carrying closed type fine flow solenoid valve 5 in parallel to the valve 4. In the case of use, the valve is left as adjusted to about one of several fractions a charging pressure of a setting pressure cylinder 1 of the valve 6. When a power supply of a control device D is lost, the valves 4, 5 are opened to release a large amount of nitrogen gas through the valve 3 from a cylinder unit B. When a cylinder pressure is decreased to a prescribed value or less, the valve 6 is closed, thereafter to supply a fine flow amount of nitrogen gas to the cell A through only the orifice 7. Accordingly, even without restoring the power supply for several tens of hours, catalyst protecting purge gas is maintained.

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、燃料電池の運転を停止
した際に、内部に残留した可燃ガスをパージ(置換)す
るための装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for purging (replacing) the combustible gas remaining inside when the operation of a fuel cell is stopped.

【0002】[0002]

【従来の技術】燃料電池は、天然ガスを水素に変換する
燃料改質装置、水素及び酸素を反応させて電気を取り出
すセルスタック等で構成されているが、運転を停止する
際には安全のために内部の可燃ガスをパージする必要が
あり、また可燃ガスをパージしたのちも、触媒が酸素や
水蒸気と接触して損傷しないように窒素ガスによって保
護する必要がある。図1は、従来の燃料電池パージ装置
を示したもので、複数の窒素ボンベ1が連結されたボン
ベ集合管2に減圧弁3を接続してなるボンベユニットB
を、通電閉型の主電磁弁4を介して燃料電池本体Cに接
続すると共に、主電磁弁4と並列に通電閉型の微流量電
磁弁5を接続したものであり、運転を停止する場合に
は、まず大流量の主電磁弁4を開き、一定時間窒素ガス
を流して系内の可燃ガスをパージしたのち弁4を閉じ、
以後は触媒保護用の微流量電磁弁5のみで運転停止期間
中連続して又は断続的に窒素ガスを流し、燃料改質装置
やセルスタックの触媒を保護するようになっている。主
電磁弁4及び微流量電磁弁5に通電閉型を用いているの
は、停電時に電磁弁を開いてパージ用ガスを流し、安全
を確保するためである。
2. Description of the Related Art A fuel cell is composed of a fuel reformer for converting natural gas into hydrogen, a cell stack for reacting hydrogen and oxygen to take out electricity, and it is safe to stop the operation. Therefore, it is necessary to purge the combustible gas inside, and also after purging the combustible gas, it is necessary to protect the catalyst with nitrogen gas so as not to damage the catalyst by contacting with oxygen or water vapor. FIG. 1 shows a conventional fuel cell purging device, which is a cylinder unit B in which a pressure reducing valve 3 is connected to a cylinder collecting pipe 2 to which a plurality of nitrogen cylinders 1 are connected.
Is connected to the fuel cell main body C via the energization-closed type main solenoid valve 4, and the energization-closed type minute flow rate solenoid valve 5 is connected in parallel with the main solenoid valve 4 to stop the operation. First, the main solenoid valve 4 with a large flow rate is opened, nitrogen gas is allowed to flow for a certain period of time to purge the combustible gas in the system, and then the valve 4 is closed.
After that, only the minute flow rate solenoid valve 5 for protecting the catalyst is used to continuously or intermittently flow the nitrogen gas during the operation stop period to protect the catalyst of the fuel reformer and the cell stack. The main solenoid valve 4 and the minute flow solenoid valve 5 are energized closed type in order to ensure safety by opening the solenoid valve and flowing purge gas at the time of power failure.

【0003】[0003]

【発明が解決しようとする課題】しかし上述の構成にお
いて、停電あるいは故障等で燃料電池の制御用電源が喪
失した場合には、通電閉型の電磁弁4,5は開となるの
で、系内の可燃ガスは窒素ガスで置換されて安全が確保
されるが、電源喪失時間があまり長くなると、ボンベに
蓄積されていた窒素ガスがすべて使い尽くされてしま
い、その後は触媒保護用のパージを続行できなくなる。
またボンベユニットBのパージ制御を停電中に行おうと
すれば、例えば電池式の流量センサ、タイマあるいはバ
ルブ等をボンベユニット側に備えて、パージガスの大量
放出を可燃ガスパージに必要な一定時間(例えば10
分)に制限する方法が考えられるが、コストがかかる上
に、運転停止が稀であることを考えると信頼性の点でも
問題がある。従って係員は真夜中でも現場に駆けつけ
て、窒素ボンベが空になるまで(例えば停電後30分以
内)に、新しいボンベと取り替えなければならないとい
う問題があった。本発明は上述の問題点を解消し、電源
喪失時間が長くなっても触媒保護に支障を来すおそれの
ない燃料電池のパージ装置を提供することを目的とする
ものである。
However, in the above-mentioned structure, when the power source for controlling the fuel cell is lost due to a power failure or a failure, the solenoid valves 4 and 5 of the energized closed type are opened, so that the internal system is closed. The combustible gas is replaced with nitrogen gas to ensure safety, but if the power loss time is too long, the nitrogen gas accumulated in the cylinder will be exhausted, and the purging for catalyst protection will continue after that. become unable.
If the purge control of the cylinder unit B is to be performed during a power failure, for example, a battery type flow sensor, a timer, a valve, or the like is provided on the cylinder unit side, and a large amount of purge gas is released for a fixed time (for example, 10
However, in addition to the high cost, there is a problem in terms of reliability when considering that operation is rare. Therefore, there was a problem that the staff member had to rush to the site even at midnight and replace the nitrogen cylinder with a new one before the nitrogen cylinder became empty (for example, within 30 minutes after the power failure). SUMMARY OF THE INVENTION It is an object of the present invention to solve the above-mentioned problems and to provide a fuel cell purging device that does not hinder the protection of the catalyst even if the power loss time becomes long.

【0004】[0004]

【課題を解決するための手段】本発明は、図2に示すよ
うに、複数の窒素ボンベ1が連結されたボンベ集合管2
に減圧弁3を介装してなるボンベユニットBを、可燃ガ
スパージ用の通電閉型主電磁弁4を介して燃料電池本体
Cに接続すると共に、主電磁弁4と並列に触媒保護用の
通電閉型微量電磁弁5を接続し燃料電池の運転停止時に
上記主電磁弁を開いて一定時間の可燃ガスパージを行っ
たのちは微流量電磁弁のみを開いて触媒保護を行うよう
にした燃料電池用パージ装置において、上記減圧弁3の
入口側のボンベ集合管2に一次圧力調整弁6を介装し、
この一次圧力調整弁6と並列に微流量のバルブ乃至オリ
フィス7を設けたものである。
According to the present invention, as shown in FIG. 2, a cylinder collecting pipe 2 in which a plurality of nitrogen cylinders 1 are connected.
A cylinder unit B having a pressure reducing valve 3 interposed therein is connected to a fuel cell main body C via an energized closed main solenoid valve 4 for purging combustible gas, and in parallel with the main solenoid valve 4, energization for catalyst protection is conducted. For a fuel cell in which a closed type small amount solenoid valve 5 is connected and the main solenoid valve is opened when the operation of the fuel cell is stopped to perform a combustible gas purge for a certain period of time and then only the minute flow solenoid valve is opened to protect the catalyst. In the purging device, a primary pressure adjusting valve 6 is provided in the cylinder collecting pipe 2 on the inlet side of the pressure reducing valve 3,
A minute flow rate valve or orifice 7 is provided in parallel with the primary pressure adjusting valve 6.

【0005】[0005]

【作用】上述の構成によれば、一次圧力調整弁6の設定
圧力をボンベ1の充填圧力(150kg/cm2 G)の
数分の一程度(例えば20kg/cm2 G)の値に調整
しておけば、電源喪失が発生して窒素が大量放出された
場合にも、触媒保護のためには十分な量の窒素ガスを残
して一次圧力調整弁6が遮断されるので、その後もオリ
フィス7を通して微流量の窒素ガスによるパージを確保
することができ、従って電源喪失が長時間に及んでも触
媒が損傷するおそれはない。
According to the above construction, the set pressure of the primary pressure adjusting valve 6 should be adjusted to a value which is a fraction of the filling pressure (150 kg / cm 2 G) of the cylinder 1 (for example, 20 kg / cm 2 G). For example, even if a large amount of nitrogen is released due to power loss, the primary pressure regulating valve 6 is shut off leaving a sufficient amount of nitrogen gas for catalyst protection. A purge of nitrogen gas at a flow rate can be ensured, and therefore there is no risk of catalyst damage even if the power supply is lost for a long time.

【0006】[0006]

【実施例】図2は本発明による燃料電池パージ装置の一
実施例を示したもので、ボンベユニットBには複数の窒
素ガスボンベ1が連結されたボンベ集合管2に減圧弁3
が介装されており、この減圧弁3によって通常充填時1
50kg/cm2 Gのボンベ圧力が5〜10kg/cm
2 Gに減圧されて燃料電池Aへ送られている。この減圧
弁3の入口側のボンベ集合管2に一次圧力調整弁6が介
装され、この一次圧力調整弁6と並列に微流量のバルブ
乃至オリフィス7が設けられており、このボンベユニッ
トBが接続される燃料電池A側では、接続口に通電時に
弁の閉じる通電閉型主電磁弁4が介装され、この主電磁
弁4と並列に触媒保護用の通電閉型微量電磁弁5が接続
されている。なお図中8は主流量調整弁、9は微流量調
整弁である。
FIG. 2 shows an embodiment of the fuel cell purging device according to the present invention. A cylinder unit B is connected to a plurality of nitrogen gas cylinders 1 and a pressure reducing valve 3 is connected to a cylinder collecting pipe 2.
The pressure reducing valve 3 is used for normal filling 1
50kg / cm2 G cylinder pressure is 5-10kg / cm
Depressurized to 2 G and sent to fuel cell A. A primary pressure adjusting valve 6 is provided in the cylinder collecting pipe 2 on the inlet side of the pressure reducing valve 3, and a minute flow valve or orifice 7 is provided in parallel with the primary pressure adjusting valve 6, and the cylinder unit B is On the side of the fuel cell A to be connected, an energized closed type main solenoid valve 4 that closes the valve when energized is inserted in the connection port, and an energized closed type minute solenoid valve 5 for catalyst protection is connected in parallel with this main solenoid valve 4. Has been done. In the figure, 8 is a main flow rate adjusting valve, and 9 is a fine flow rate adjusting valve.

【0007】使用の際には、一次圧力調整弁6の設定圧
力をボンベ1の充填圧の数分の一程度の値(20〜30
kg/cm2 G)に調整しておく。いま制御装置Dの電
源が喪失すると、通電閉型の主電磁弁4及び微流量電磁
弁5が開いて、ボンベユニットBから窒素が減圧弁3の
二次圧力(例えば6kg/cm2 G)で大量放出される
が、例えば30分後にボンベ圧力が20kg/cm2 G
以下に低下すると、一次圧力調整弁6がこれを検出して
閉弁し、以後はオリフィス7のみを通して微流量の窒素
ガスが6kg/cm2 Gで燃料電池Aに供給され、以後
数10時間は電源が回復しなくても触媒保護用パージガ
スが維持される。図中10は圧力計、11は安全弁であ
る。
In use, the set pressure of the primary pressure control valve 6 is a value (20 to 30) which is a fraction of the filling pressure of the cylinder 1.
Adjust to kg / cm2 G). When the power supply of the control unit D is lost, the energization-closed main solenoid valve 4 and the minute flow solenoid valve 5 are opened, and a large amount of nitrogen from the cylinder unit B is generated at the secondary pressure of the pressure reducing valve 3 (for example, 6 kg / cm 2 G). It is released, but after 30 minutes, the cylinder pressure is 20 kg / cm 2 G
When the pressure drops below, the primary pressure regulating valve 6 detects it and closes it. Thereafter, a small flow rate of nitrogen gas is supplied to the fuel cell A at 6 kg / cm 2 G through only the orifice 7, and then the power is supplied for several tens of hours. Even if the gas does not recover, the purge gas for catalyst protection is maintained. In the figure, 10 is a pressure gauge and 11 is a safety valve.

【0008】図3は従来構成による動作(実線)と本発
明構成による動作(破線)とを比較したもので、(a)
はボンベ残圧、(b)はボンベからの流出量を示してい
る。図1の従来構成によれば、まずt0 で電源が喪失す
ると、燃料電池側の両電磁弁4,5が開くために、パー
ジガスは(b)に示すように、主流量調整弁8で設定さ
れている可燃ガスパージ用流量で流れ、t1 で可燃ガス
のパージが完了した後も、主電磁弁5の制御が行われな
いために、減圧弁3により一定圧力(例えば6kg/c
m2 G)に維持されながらほぼ同一流量で流れ続ける。
そして(a)に示すように、t3 において一次圧力が6
kg/cm2 G以下になったのち、しばらくして流量が
0となる。これに対して図2の本発明構成では、ボンベ
残圧が比較的高い(例えば20kg/cm2 G)時点す
なわち(a)におけるt2 で一次圧力調整弁6が閉弁
し、以後は(b)に破線で示したように、微量調整弁7
を通ってごく僅かな窒素ガスが流出するのみなので、
(a)に破線で示すように、以後少なくとも数時間は触
媒保護用のパージガスを継続して供給することができる
のである。
FIG. 3 compares the operation of the conventional configuration (solid line) with the operation of the present invention (broken line).
Indicates the cylinder residual pressure, and (b) indicates the outflow amount from the cylinder. According to the conventional configuration of FIG. 1, when the power source is lost at t0, the solenoid valves 4 and 5 on the fuel cell side are opened, so that the purge gas is set by the main flow rate adjusting valve 8 as shown in (b). Flow at a flow rate for purging combustible gas, and even after the purging of combustible gas is completed at t1, since the main solenoid valve 5 is not controlled, the pressure reducing valve 3 maintains a constant pressure (for example, 6 kg / c).
m2 G) and keep flowing at almost the same flow rate.
Then, as shown in (a), the primary pressure is 6 at t3.
After becoming less than kg / cm 2 G, the flow rate becomes 0 after a while. On the other hand, in the configuration of the present invention shown in FIG. 2, the primary pressure adjusting valve 6 is closed at t2 when the cylinder residual pressure is relatively high (for example, 20 kg / cm2 G), that is, at t2 in (a), and thereafter in (b). As indicated by the broken line, the fine adjustment valve 7
Since only a small amount of nitrogen gas flows out through the
As indicated by the broken line in (a), the purge gas for protecting the catalyst can be continuously supplied for at least several hours thereafter.

【0009】[0009]

【発明の効果】本発明によれば上述のように、一次圧力
調整弁6の設定圧力をボンベ1の充填圧の数分の一程度
の値に調整しておくことによって、電源喪失時に窒素ガ
スが可燃ガスパージ必要量を超えて大量に放出された場
合にも、触媒保護に十分な量を残して一次圧力調整弁6
が閉弁し、以後は微流量バルブ又はオリフィス7を通し
て微流量の窒素ガスを長時間流し続けることができるの
で、電源喪失後長時間復電しなくても触媒が損傷するお
それがなく、また従来のように停電時に係員がボンベの
取り替えに駆けつける必要がなくなったという利点があ
る。
According to the present invention, as described above, by adjusting the set pressure of the primary pressure adjusting valve 6 to a value which is a fraction of the filling pressure of the cylinder 1, nitrogen gas is lost when power is lost. Even if a large amount of exhaust gas is released in excess of the required amount of combustible gas purge, the primary pressure regulating valve 6 is left with a sufficient amount for catalyst protection.
Is closed, and thereafter, a small flow rate of nitrogen gas can be continued to flow for a long time through the fine flow rate valve or orifice 7. Therefore, there is no risk of damage to the catalyst even if power is not restored for a long time after power loss, and There is an advantage that the staff does not have to rush to replace the cylinder at the time of power failure like this.

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

【図1】従来のこの種の装置の系統図である。1 is a system diagram of a conventional device of this type.

【図2】本発明装置の系統図である。FIG. 2 is a system diagram of the device of the present invention.

【図3】本発明装置の動作を従来例と比較して示したも
ので、(a)はボンベ残圧の変化、(b)はパージガス
流量の変化を示すグラフである。
FIG. 3 is a graph showing the operation of the device of the present invention in comparison with a conventional example, in which (a) is a graph showing a change in cylinder residual pressure and (b) is a graph showing a change in purge gas flow rate.

【符号の説明】[Explanation of symbols]

1 窒素ボンベ 2 ボンベ集合管 3 減圧弁 4 主電磁弁 5 微量電磁弁 6 一次圧力調整弁 7 バルブ又はオリフィス 8 主流量調整弁 9 微量流量調整弁 10 圧力計 11 安全弁 A 燃料電池 B ボンベユニット C 燃料電池本体 D 制御装置 1 Nitrogen cylinder 2 Cylinder collecting pipe 3 Pressure reducing valve 4 Main solenoid valve 5 Micro solenoid valve 6 Primary pressure regulating valve 7 Valve or orifice 8 Main flow regulating valve 9 Micro flow regulating valve 10 Pressure gauge 11 Safety valve A Fuel cell B Cylinder unit C Fuel Battery body D control device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 窒素ボンベを連結したボンベ集合管に減
圧弁を介装してなるボンベユニットを、通電閉型の主電
磁弁を介して燃料電池本体に接続すると共に、主電磁弁
と並列に通電閉型の微流量電磁弁を接続し、燃料電池の
運転停止時に上記主電磁弁を開いて一定時間の可燃ガス
パージを行ったのちは微流量電磁弁のみを開いて触媒保
護を行うようにした燃料電池パージ装置において、上記
減圧弁の入口側のボンベ集合管に一次圧力調整弁を介装
し、この一次圧力調整弁と並列に微流量のバルブ乃至オ
リフィスを設けて成る燃料電池パージ装置。
1. A cylinder unit in which a pressure reducing valve is installed in a cylinder collecting pipe to which a nitrogen cylinder is connected is connected to a fuel cell main body through a main solenoid valve of a current-closed type, and in parallel with the main solenoid valve. An energization-closed type minute flow solenoid valve was connected, and when the fuel cell was not operating, the main solenoid valve was opened to purge combustible gas for a certain period of time, and then only the minute flow solenoid valve was opened to protect the catalyst. In the fuel cell purging device, a primary pressure adjusting valve is provided in the cylinder collecting pipe on the inlet side of the pressure reducing valve, and a minute flow valve or orifice is provided in parallel with the primary pressure adjusting valve.
JP08573494A 1994-03-30 1994-03-30 Fuel cell purge device Expired - Fee Related JP3360766B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08573494A JP3360766B2 (en) 1994-03-30 1994-03-30 Fuel cell purge device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08573494A JP3360766B2 (en) 1994-03-30 1994-03-30 Fuel cell purge device

Publications (2)

Publication Number Publication Date
JPH07272739A true JPH07272739A (en) 1995-10-20
JP3360766B2 JP3360766B2 (en) 2002-12-24

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JP2002056853A (en) * 2000-08-14 2002-02-22 Sony Corp Emergency power generation and water supply system
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JP2004206898A (en) * 2002-12-24 2004-07-22 Equos Research Co Ltd Fuel cell system
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JP2013182720A (en) * 2012-02-29 2013-09-12 Mitsubishi Heavy Ind Ltd Sofc combined power generation system and operation method of the same
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US11738305B2 (en) 2012-08-30 2023-08-29 Element 1 Corp Hydrogen purification devices

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6602628B2 (en) 2000-03-24 2003-08-05 Honda Giken Kogyo Kabushiki Kaisha Control system for fuel cell
JP2002056853A (en) * 2000-08-14 2002-02-22 Sony Corp Emergency power generation and water supply system
JP2004206898A (en) * 2002-12-24 2004-07-22 Equos Research Co Ltd Fuel cell system
JP4599796B2 (en) * 2002-12-24 2010-12-15 株式会社エクォス・リサーチ Fuel cell system
JP2013520673A (en) * 2010-02-26 2013-06-06 ディーエイチ テクノロジーズ デベロップメント プライベート リミテッド Gas delivery system for mass spectrometer reaction and collision cells
JP2013182720A (en) * 2012-02-29 2013-09-12 Mitsubishi Heavy Ind Ltd Sofc combined power generation system and operation method of the same
US11879178B2 (en) 2021-03-18 2024-01-23 Kabushiki Kaisha Toshiba Electrochemical device

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