JP3360766B2 - Fuel cell purge device - Google Patents

Fuel cell purge device

Info

Publication number
JP3360766B2
JP3360766B2 JP08573494A JP8573494A JP3360766B2 JP 3360766 B2 JP3360766 B2 JP 3360766B2 JP 08573494 A JP08573494 A JP 08573494A JP 8573494 A JP8573494 A JP 8573494A JP 3360766 B2 JP3360766 B2 JP 3360766B2
Authority
JP
Japan
Prior art keywords
valve
fuel cell
cylinder
pressure
solenoid valve
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 - Fee Related
Application number
JP08573494A
Other languages
Japanese (ja)
Other versions
JPH07272739A (en
Inventor
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)

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 an apparatus for purging (replacing) combustible gas remaining inside a fuel cell when the operation of the 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 extracting electricity by reacting hydrogen and oxygen, and the like. Therefore, it is necessary to purge the internal combustible gas, and after purging the combustible gas, it is necessary to protect the catalyst with nitrogen gas so as not to be damaged by contact with oxygen or water vapor. FIG. 1 shows a conventional fuel cell purging apparatus, in which 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 body C via the energized closed main solenoid valve 4 and an energized closed micro flow 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 flown for a certain time to purge the combustible gas in the system, and then the valve 4 is closed.
Thereafter, nitrogen gas is continuously or intermittently flowed during the operation stop period only by the micro flow rate solenoid valve 5 for protecting the catalyst, thereby protecting the catalyst of the fuel reformer and the cell stack. The reason why the main solenoid valve 4 and the minute flow rate solenoid valve 5 are energized and closed is to open the solenoid valves at the time of a power failure and to flow purge gas to ensure safety.

【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 configuration, when the power supply for controlling the fuel cell is lost due to a power failure or a failure, the energized closed solenoid valves 4 and 5 are opened. The flammable gas is replaced with nitrogen gas to ensure safety, but if the power loss time is too long, all the nitrogen gas accumulated in the cylinder will be exhausted, and then purging to protect the catalyst will continue. become unable.
If the purging 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 so that a large amount of purge gas is discharged for a certain period of time (for example, 10 minutes) required for combustible gas purging.
However, there is a problem in terms of reliability in view of the fact that the operation is rarely stopped in addition to the cost. Therefore, there was a problem that the attendant rushed to the site even at midnight and had to replace it with a new cylinder before the nitrogen cylinder became empty (for example, within 30 minutes after a 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 apparatus which does not hinder catalyst protection even when the power supply loss time is 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
入口側に一定値以上のガス圧力で開弁する一次圧力調整
弁6を介装し、上記一定値をボンベ充填圧の数分の一程
度に設定すると共に、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 electromagnetic valve 4 for combustible gas purging, and an energization for catalyst protection is performed in parallel with the main electromagnetic valve 4. For a fuel cell in which a closed micro solenoid valve 5 is connected, the main solenoid valve is opened when the operation of the fuel cell is stopped, combustible gas is purged for a certain time, and then only the micro flow solenoid valve is opened to protect the catalyst. In the purge device, a primary pressure adjustment for opening the inlet side of the pressure reducing valve 3 with a gas pressure of a certain value or more.
With the valve 6 interposed, the above-mentioned constant value is set to a fraction of the cylinder filling pressure.
The primary pressure regulating valve 6 is provided with a valve or an orifice 7 having a small flow rate in parallel with the primary pressure regulating 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-mentioned structure, the set pressure of the primary pressure regulating valve 6 can be adjusted to a value which is about a fraction (for example, 20 kg / cm2 G) of the filling pressure of the cylinder 1 (150 kg / cm2 G). For example, even if a power loss occurs and a large amount of nitrogen is released, the primary pressure regulating valve 6 is shut off leaving a sufficient amount of nitrogen gas for protection of the catalyst. Purging with a flow of nitrogen gas can be ensured, so that there is no risk of damaging the catalyst over long periods of power loss.

【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 a fuel cell purging apparatus according to the present invention. In a cylinder unit B, a pressure reducing valve 3 is connected to a cylinder collecting pipe 2 to which a plurality of nitrogen gas cylinders 1 are connected.
The pressure reducing valve 3 allows the normal filling 1
50kg / cm2 G cylinder pressure 5-10kg / cm
The pressure is reduced to 2 G and sent to the fuel cell A. A primary pressure regulating valve 6 is interposed in the cylinder collecting pipe 2 on the inlet side of the pressure reducing valve 3, and a valve or an orifice 7 having a small flow rate is provided in parallel with the primary pressure regulating valve 6. On the side of the fuel cell A to be connected, an energized closed main solenoid valve 4 that closes the valve when energized at the connection port, and an energized closed micro solenoid valve 5 for catalyst protection is connected in parallel with the main solenoid valve 4. Have been. In the figure, reference numeral 8 denotes a main flow control valve, and 9 denotes a fine flow control 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 regulating valve 6 is set to a value which is a fraction of the filling pressure of the cylinder 1 (20 to 30).
kg / cm2 G). When the power supply of the control device D is lost, the main solenoid valve 4 and the minute flow rate solenoid valve 5, which are energized and closed, are opened, and a large amount of nitrogen is released from the cylinder unit B at the secondary pressure of the pressure reducing valve 3 (for example, 6 kg / cm2 G). It is released, for example, after 30 minutes, the cylinder pressure becomes 20 kg / cm 2 G
When the pressure drops to below, the primary pressure regulating valve 6 detects this and closes the valve. Thereafter, a small flow rate of nitrogen gas is supplied to the fuel cell A at 6 kg / cm 2 G only through the orifice 7, and the power supply is maintained for several tens of hours thereafter. Is maintained, the purge gas for protecting the catalyst 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 shows a comparison between the operation according to the conventional configuration (solid line) and the operation according to the configuration of the present invention (dashed line).
Indicates the cylinder residual pressure, and (b) indicates the amount of outflow from the cylinder. According to the conventional configuration shown in FIG. 1, when the power supply is lost at t0, the two solenoid valves 4 and 5 on the fuel cell side are opened, so that the purge gas is set by the main flow control valve 8 as shown in FIG. Since the main solenoid valve 5 is not controlled even after the combustible gas has been purged at t1, the pressure is reduced by the pressure reducing valve 3 to a constant pressure (for example, 6 kg / c).
m2 G) and continue to flow at substantially the same flow rate.
Then, as shown in (a), at t3, the primary pressure becomes 6
After the pressure becomes less than kg / cm 2 G, the flow rate becomes 0 shortly thereafter. On the other hand, in the configuration of the present invention shown in FIG. 2, the primary pressure regulating valve 6 is closed at the time when the cylinder residual pressure is relatively high (for example, 20 kg / cm @ 2 G), that is, at t2 in FIG. As indicated by the dashed line, the minute adjustment valve 7
Only a small amount of nitrogen gas flows out through
As shown 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。また上記一次圧力調整弁6は、燃料電池設備A側の
制御装置Dによって制御されるものではなく、ガス圧力
のみによって受動的かつ機械的に動作するものであるか
ら、異常発生時における信頼性がきわめて高いという利
点がある。
According to the present invention, as described above, by setting the set pressure of the primary pressure regulating valve 6 to a value which is about a fraction of the filling pressure of the cylinder 1, the nitrogen gas is supplied when the power is lost. Is released in a large amount exceeding the required amount of the combustible gas purge, the primary pressure regulating valve 6 is left with a sufficient amount for protecting the catalyst.
The valve closes, and thereafter a minute flow of nitrogen gas can be continued to flow through the minute flow valve or the orifice 7 for a long time. There is an advantage that it is no longer necessary for the attendant to rush to replace the cylinder in the event of a power outage. Further, the primary pressure regulating valve 6 is connected to the fuel cell equipment A side.
Not controlled by control device D, gas pressure
Only passively and mechanically operated by
Is extremely reliable in the event of an abnormality.
There is a point.

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

【図1】従来のこの種の装置の系統図である。FIG. 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。
FIGS. 3A and 3B show the operation of the apparatus of the present invention in comparison with a conventional example, in which FIG. 3A is a graph showing a change in cylinder residual pressure, and FIG. 3B 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 DESCRIPTION OF SYMBOLS 1 Nitrogen cylinder 2 Cylinder collecting pipe 3 Pressure reducing valve 4 Main solenoid valve 5 Micro solenoid valve 6 Primary pressure control valve 7 Valve or orifice 8 Main flow control valve 9 Micro flow control valve 10 Pressure gauge 11 Safety valve A Fuel cell B Bomb unit C Fuel Battery body D control device

Claims (1)

(57)【特許請求の範囲】(57) [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
減圧弁の入口側に一定値以上のガス圧力で開弁する一次
圧力調整弁を介装し、上記一定値をボンベ充填圧の数分
の一程度に設定すると共に、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 having a pressure reducing valve interposed in a cylinder collecting pipe connected to a nitrogen cylinder is connected to a fuel cell main body through a main solenoid valve of an energized closed type, and is connected in parallel with the main solenoid valve. A micro-flow solenoid valve of an energized closed type was connected, and when the operation of the fuel cell was stopped, the main solenoid valve was opened to perform flammable gas purging for a certain time, and then only the micro-flow solenoid valve was opened to protect the catalyst. In the fuel cell purge device, a primary valve that opens at a gas pressure equal to or higher than a certain value at an inlet side of the pressure reducing valve.
With the pressure regulating valve interposed, keep the above constant value several minutes of the cylinder filling pressure.
A fuel cell purging apparatus comprising a valve or an orifice with a small flow rate set in parallel with the primary pressure regulating 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 JPH07272739A (en) 1995-10-20
JP3360766B2 true JP3360766B2 (en) 2002-12-24

Family

ID=13867077

Family Applications (1)

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

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Country Link
JP (1) JP3360766B2 (en)

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US11738305B2 (en) 2012-08-30 2023-08-29 Element 1 Corp Hydrogen purification devices

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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
JP4599796B2 (en) * 2002-12-24 2010-12-15 株式会社エクォス・リサーチ Fuel cell system
US8373117B2 (en) * 2010-02-26 2013-02-12 Dh Technologies Development Pte. Ltd. Gas delivery system for mass spectrometer reaction and collision cells
JP5787791B2 (en) * 2012-02-29 2015-09-30 三菱日立パワーシステムズ株式会社 SOFC combined power generation apparatus and operation method thereof
JP2022143974A (en) 2021-03-18 2022-10-03 株式会社東芝 electrochemical device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11738305B2 (en) 2012-08-30 2023-08-29 Element 1 Corp Hydrogen purification devices

Also Published As

Publication number Publication date
JPH07272739A (en) 1995-10-20

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