JP2001283884A - Fuel cell generating device - Google Patents

Fuel cell generating device

Info

Publication number
JP2001283884A
JP2001283884A JP2000098486A JP2000098486A JP2001283884A JP 2001283884 A JP2001283884 A JP 2001283884A JP 2000098486 A JP2000098486 A JP 2000098486A JP 2000098486 A JP2000098486 A JP 2000098486A JP 2001283884 A JP2001283884 A JP 2001283884A
Authority
JP
Japan
Prior art keywords
water
fuel cell
blowdown
steam separator
generated
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
JP2000098486A
Other languages
Japanese (ja)
Other versions
JP3741257B2 (en
Inventor
Harumasa Takeda
治正 竹田
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
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP2000098486A priority Critical patent/JP3741257B2/en
Publication of JP2001283884A publication Critical patent/JP2001283884A/en
Application granted granted Critical
Publication of JP3741257B2 publication Critical patent/JP3741257B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a fuel cell generating device that prevents the trouble of reserved water flowing out totally from the steam separator at the time of the stoppage of the device and simplifies the blowdown circuit as well as reducing total cost. SOLUTION: The fuel cell generating device comprises a fuel cell body 1 which is mounted with a cooling plate flowing cooling water, a steam separator 5 separating the hot cooling water discharged from the cooling plate into steam and water and a generated water collector 7 for collecting the water generated in the fuel cell. The steam separator 5 is equipped with a blowdown circuit 100, which discharges the internal reserved water to the generated water collector 7. And the blowdown circuit is equipped with a blowdown water pressure control means having a thin pipe 10 of a smaller pipe sectional area than the main pipe of the circuit. A blowdown water drainage port 13 discharging into the generated water collector is installed at a higher position than a water level control position 12.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、燃料電池発電装
置における燃料電池冷却水系、特に水蒸気分離器が備え
るブローダウン回路の構成に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel cell cooling water system in a fuel cell power generator, and more particularly to a blow-down circuit provided in a steam separator.

【0002】[0002]

【従来の技術】周知のとおり、リン酸型燃料電池は、反
応ガスとしての燃料ガス(例えば、水素)および酸化剤
ガス(例えば、空気)を電極触媒層を備えた燃料極およ
び酸化剤極に連続的に供給して、燃料のもつエネルギー
を電気化学的に電気エネルギーに変換するものである。
図2は、リン酸型水冷式燃料電池を用いた従来の燃料電
池発電装置の燃料ガス供給系、空気供給系、ならびに冷
却水系の基本構成を示す模式図である。
2. Description of the Related Art As is well known, a phosphoric acid type fuel cell applies a fuel gas (for example, hydrogen) and an oxidant gas (for example, air) as reaction gas to a fuel electrode and an oxidant electrode provided with an electrode catalyst layer. It is supplied continuously to electrochemically convert the energy of the fuel into electric energy.
FIG. 2 is a schematic diagram showing a basic configuration of a fuel gas supply system, an air supply system, and a cooling water system of a conventional fuel cell power generator using a phosphoric acid type water-cooled fuel cell.

【0003】模式的に表示した燃料電池本体1は、リン
酸を保持した電解質層を燃料極と空気極で挟持して形成
した単セルを積層して構成されており、複数層ごとに発
電に伴う発熱を除去する冷却板が介装されている。燃料
電池本体1の燃料極へは、原燃料を水添脱硫器4で脱硫
し、エゼクタポンプ3で水蒸気と混合し、燃料改質器2
で改質された水素濃度の高い燃料ガスが供給される。
The fuel cell main body 1 schematically shown is formed by stacking single cells formed by sandwiching an electrolyte layer holding phosphoric acid between a fuel electrode and an air electrode, and generating power for each of a plurality of layers. A cooling plate for removing the accompanying heat generation is provided. The raw fuel is desulfurized by the hydrodesulfurizer 4 to the fuel electrode of the fuel cell main body 1, mixed with steam by the ejector pump 3, and supplied to the fuel reformer 2.
The fuel gas having a high hydrogen concentration reformed by the above is supplied.

【0004】すなわち、原燃料を水添脱硫器4に導入し
て水素を添加し、付臭剤として原燃料に含まれている硫
黄を吸着除去したのち、エゼクタポンプ3において水蒸
気分離器5より送られる水蒸気と混合し、燃料改質器2
に送って加熱して触媒反応によって水素濃度の高い燃料
ガスを生成し、燃料極へと供給している。なお、燃料ガ
スを燃料極へと供給する配管には、水添脱硫器4に導入
する原燃料に燃料ガスの一部を再循環させて混合するた
めのリサイクルガス回路が接続されており、再循環させ
た燃料ガスに含まれる水素を水添脱硫器4における脱硫
に有効利用するよう構成されている。
That is, the raw fuel is introduced into the hydrodesulfurizer 4 to add hydrogen, and the sulfur contained in the raw fuel as an odorant is adsorbed and removed, and then sent from the steam separator 5 in the ejector pump 3. Mixed with the steam to be recovered, and the fuel reformer 2
To generate a fuel gas having a high hydrogen concentration by a catalytic reaction and supply it to the fuel electrode. A pipe for supplying the fuel gas to the fuel electrode is connected to a recycle gas circuit for recirculating and mixing a part of the fuel gas with the raw fuel introduced into the hydrodesulfurizer 4. The hydrogen contained in the circulated fuel gas is configured to be effectively used for desulfurization in the hydrodesulfurizer 4.

【0005】また、燃料極より反応に寄与しないで排出
される残存水素を含む燃料極オフガスと外部よりブロア
によって供給される燃焼空気を、燃料改質器2の燃焼器
に導入し、燃焼させることにより、燃料改質器2の通流
ガスを加熱している。一方、燃料電池本体1の空気極へ
は、反応空気をブロアで取り込んで供給している。空気
極より排出される空気極オフガスには、電気化学反応に
伴って生じた反応生成水が含まれ、また燃料改質器2の
燃焼器より排出される燃焼排ガスには燃焼に伴って生じ
た燃焼生成水が含まれている。したがって、空気極オフ
ガスと燃焼排ガスは生成水回収装置7へと送られ、生成
水を回収したのち外部へ排出されるように構成されてい
る。
The fuel electrode off-gas containing residual hydrogen discharged from the fuel electrode without contributing to the reaction and the combustion air supplied from the outside by a blower are introduced into the combustor of the fuel reformer 2 and burned. With this, the gas flowing through the fuel reformer 2 is heated. On the other hand, the reaction air is taken in and supplied to the air electrode of the fuel cell body 1 by a blower. The air electrode off-gas discharged from the air electrode contains reaction product water generated by the electrochemical reaction, and the combustion exhaust gas discharged from the combustor of the fuel reformer 2 is generated by combustion. Contains water produced by combustion. Therefore, the air electrode off-gas and the combustion exhaust gas are sent to the generated water recovery device 7, where the generated water is recovered and then discharged to the outside.

【0006】燃料電池本体の冷却板には水蒸気分離器5
より冷却水を供給して、発電に伴って発生する熱を除去
し、燃料電池本体の温度を所定の運転温度に維持してい
る。冷却板において発熱を受けて高温となった冷却水
は、冷却水冷却器6により冷却されたのち、水蒸気分離
器5に戻され、水蒸気と水とに分離される。なお、冷却
水冷却器6の冷却によって得られた熱は外部に取り出さ
れ有効利用される。水蒸気分離器5で分離された水蒸気
は、前述のようにエゼクタポンプ3に送られ、改質に用
いられる。また、エゼクタポンプ3へ水蒸気を供給する
ことにより減少する水量を補うため、生成水回収装置7
で回収された生成水を水処理装置8で純化して導入して
いる。
A steam separator 5 is provided on the cooling plate of the fuel cell body.
More cooling water is supplied to remove heat generated by power generation, and the temperature of the fuel cell main body is maintained at a predetermined operating temperature. The cooling water, which has been heated to a high temperature by receiving heat from the cooling plate, is cooled by the cooling water cooler 6 and then returned to the steam separator 5 to be separated into steam and water. Note that heat obtained by cooling the cooling water cooler 6 is taken out to the outside and is effectively used. The steam separated by the steam separator 5 is sent to the ejector pump 3 and used for reforming as described above. Further, in order to compensate for the amount of water reduced by supplying steam to the ejector pump 3, the generated water recovery device 7
The product water collected in the above is purified by a water treatment device 8 and introduced.

【0007】さらに、水蒸気分離器5には、貯留された
水をブローダウンして生成水回収装置7へと送るブロー
ダウン回路100が設けられており、貯留水をブローダ
ウン回路より生成水回収装置7へと送り、水処理装置8
で純化して水蒸気分離器5に戻すことにより、貯留水の
水質低下を防止している。
Further, the steam separator 5 is provided with a blowdown circuit 100 for blowing down the stored water and sending it to the generated water recovery device 7. 7 and water treatment equipment 8
By returning the water to the steam separator 5, the water quality of the stored water is prevented from lowering.

【0008】上記ブロ−ダウン回路100は、図2に示
すように、ブロ−ダウン水圧力調整手段としての細管1
0と電磁遮断弁11および手動弁9を備えている。この
ブロ−ダウン回路は、運転時、常に負荷に見合った流量
の水が流れるようにしており、装置の通常停止或いは緊
急停止時には、再運転に備えた所定貯水量に応ずる所定
の水位制御位置12に到達したところで、電磁遮断弁1
1を遮断して、水蒸気分離器5の貯留水が全て流出しな
いように保護している。手動弁9は、気密試験の際の回
路遮断用に用いる。
As shown in FIG. 2, the blow-down circuit 100 includes a thin tube 1 as blow-down water pressure adjusting means.
0, an electromagnetic shutoff valve 11 and a manual valve 9. This blow-down circuit ensures that a flow of water at a flow rate corresponding to the load always flows during operation, and at the time of a normal or emergency stop of the apparatus, a predetermined water level control position 12 corresponding to a predetermined water storage amount prepared for re-operation. , The electromagnetic shut-off valve 1
1 is shut off to protect all the water stored in the steam separator 5 from flowing out. The manual valve 9 is used for shutting off a circuit at the time of an airtight test.

【0009】ところで、ブロ−ダウン水圧力調整手段と
して、上記のように細管10を用いる構成は、固定絞り
を用いる場合の水のフラッシュに伴う流量低下の問題を
解決するために、本願出願人が、特開平11−8688
9号公報において提案している構成である。前記細管1
0の内径は、水蒸気分離器5の運転中の圧力(通常約
0.6MPaG)から生成水回収装置7(大気圧)までの圧
力降下を考慮し、3mm以下が好適である。
By the way, the configuration using the thin tube 10 as the blow-down water pressure adjusting means as described above has been proposed by the applicant of the present application in order to solve the problem of the flow rate decrease caused by the flushing of water when using a fixed throttle. JP-A-11-8688
This is the configuration proposed in Japanese Patent Application Publication No. 9-99. The thin tube 1
The inner diameter of 0 is preferably 3 mm or less in consideration of the pressure drop from the pressure (normally about 0.6 MPaG) during operation of the steam separator 5 to the product water recovery device 7 (atmospheric pressure).

【0010】[0010]

【発明が解決しようとする課題】上記のように、従来の
燃料電池発電装置においては、電磁遮断弁11を遮断し
て、水蒸気分離器5の貯留水が全て流出しないように保
護しているが、下記のような問題があった。
As described above, in the conventional fuel cell power generator, the electromagnetic shutoff valve 11 is shut off to protect all the water stored in the steam separator 5 from flowing out. However, there were the following problems.

【0011】装置停止時にブロ−ダウン水に含まれる微
少なゴミ、シリカ形成物等の異物が堆積付着して電磁遮
断弁11に噛み込んだ場合、ブロ−ダウン水が出流れを
生じて、所定の水位制御位置より徐々に水位が低下し、
ついには水蒸気分離器5の貯留水が全て流出してしまう
問題があった。この場合には、再起動時の水蒸気分離器
5並びに燃料電池本体1を含む冷却水系統の水を再注入
する必要があり、再起動に時間がかかる問題があった。
When foreign matter such as minute dust and silica-forming substances contained in the blow-down water accumulates and adheres to the electromagnetic shut-off valve 11 when the apparatus is stopped, the blow-down water flows out to a predetermined level. The water level gradually drops from the water level control position of
Eventually, there is a problem that all the stored water in the steam separator 5 flows out. In this case, it is necessary to re-inject the water of the cooling water system including the steam separator 5 and the fuel cell body 1 at the time of restart, and there is a problem that it takes time to restart.

【0012】この発明は、上記問題点に鑑みてなされた
もので、この発明の課題は、装置停止時において水蒸気
分離器の貯留水が全て流出するトラブルを防止し、ブロ
ーダウン回路の簡素化を図って、トータルコストの低減
を図った燃料電池発電装置を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and an object of the present invention is to prevent a trouble that all the water stored in a steam separator flows out when the apparatus is stopped, and to simplify a blowdown circuit. SUMMARY OF THE INVENTION It is an object of the present invention to provide a fuel cell power generation device that aims to reduce the total cost.

【0013】[0013]

【課題を解決するための手段】前述の課題を解決するた
めに、この発明は、冷却水を通流する冷却板を介装して
なる燃料電池本体と、該冷却板に冷却水を供給し、冷却
板から排出される高温の冷却水を導入して水蒸気と水と
に分離する水蒸気分離器と、燃料電池における生成水を
回収するための生成水回収器とを備え、かつ、前記水蒸
気分離器は、内部の貯留水を生成水回収器へ吐出させる
ためのブローダウン回路を備え、このブローダウン回路
は、回路の主配管より管路断面積の小さな細管を用いて
なるブローダウン水圧力調整手段を備えた燃料電池発電
装置において、前記生成水回収器へ吐出するブローダウ
ン水吐出口を、前記水蒸気分離器における水位制御位置
より高い位置に設けたものとする(請求項1)。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a fuel cell main body having a cooling plate through which cooling water flows, and supplying cooling water to the cooling plate. A steam separator for introducing high-temperature cooling water discharged from the cooling plate to separate into steam and water, and a product water recovery device for recovering product water in the fuel cell; The blower has a blowdown circuit for discharging the stored water to the generated water recovery unit, and this blowdown circuit adjusts the blowdown water pressure using a small tube with a smaller cross-sectional area than the main piping of the circuit. In the fuel cell power generation apparatus provided with the means, the blowdown water discharge port discharged to the generated water recovery unit is provided at a position higher than a water level control position in the steam separator (claim 1).

【0014】上記構成においては、後に詳述するよう
に、ブローダウン回路の電磁遮断弁を省略できる。その
ため、電磁遮断弁に堆積する異物に起因し、装置停止時
に水蒸気分離器の貯留水が全て流出するトラブルがなく
なり装置の信頼性が向上できる。また、電磁遮断弁がな
い分、ブローダウン回路が簡素化され、製作時の工数、
直材費用、ソフト製作の面でコストの低減が可能とな
る。
In the above configuration, as will be described in detail later, the electromagnetic shut-off valve of the blow-down circuit can be omitted. For this reason, there is no trouble that all the water stored in the steam separator flows out when the apparatus is stopped due to the foreign matter deposited on the electromagnetic shut-off valve, and the reliability of the apparatus can be improved. Also, because there is no solenoid shut-off valve, the blowdown circuit is simplified,
It is possible to reduce costs in terms of direct material costs and software production.

【0015】さらに、前記請求項1記載の燃料電池発電
装置において、前記ブローダウン水圧力調整手段を、前
記水位制御位置より高い位置に設けたもの(請求項2)
とするのが好適である。
Further, in the fuel cell power generator according to claim 1, the blowdown water pressure adjusting means is provided at a position higher than the water level control position (claim 2).
It is preferable that

【0016】上記により、装置停止時に、ブローダウン
水圧力調整手段としての細管内部の水が排出されるの
で、水中に含まれるスケールが滞留・堆積して徐々に水
流が悪くなる問題を未然に防止することができる。
As described above, when the apparatus is stopped, the water inside the thin tube as the blowdown water pressure adjusting means is discharged, so that the problem that the scale contained in the water stays and accumulates and the water flow gradually deteriorates is prevented. can do.

【0017】[0017]

【発明の実施の形態】図1に基づき、本発明の実施例に
ついて以下にのべる。なお、図1の実施例において、図
2に示す部材と同一機能を示す部材には、同一番号を付
して説明を省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. In the embodiment shown in FIG. 1, members having the same functions as those shown in FIG. 2 are denoted by the same reference numerals, and description thereof is omitted.

【0018】図1の実施例が図2と異なる点は、水蒸気
分離器5における内部の貯留水を生成水回収器7へ吐出
させるための吐出口13を、水蒸気分離器5の水位制御
位置12よりも高い位置とするために、ブローダウン回
路100中の細管10の後段に立ち上げ配管14を設
け、図2における電磁遮断弁11を削除した点である。
なお、図1において、細管10は、水位制御位置より低
い位置に図示しているが、必要に応じ高い位置に設ける
ことは可能で、その方が前述のように好適である。ま
た、この場合には細管10の後段の配管は、下方に向け
て配管されて生成水回収器7へ接続される場合もある。
The embodiment of FIG. 1 is different from that of FIG. 2 in that a discharge port 13 for discharging the stored water in the steam separator 5 to a generated water recovery unit 7 is provided at a water level control position 12 of the steam separator 5. In order to make the position higher than that, the rising pipe 14 is provided at the subsequent stage of the thin tube 10 in the blowdown circuit 100, and the electromagnetic shutoff valve 11 in FIG.
In FIG. 1, the thin tube 10 is shown at a position lower than the water level control position, but it can be provided at a higher position if necessary, which is more preferable as described above. In this case, the pipe at the subsequent stage of the thin tube 10 may be piped downward and connected to the generated water recovery unit 7 in some cases.

【0019】上記のような構成において、通常運転時は
水蒸気分離器5出口で約0.6MPaG,細管10出口で約
0.2MPaGの水圧であれば、細管10後段の配管を水蒸
気分離器5の水位制御位置12よりも上に立ち上げてブ
ローダウン水を生成水回収器7に導入しても充分ブロー
ダウンすることが可能である。
In the above configuration, if the water pressure is about 0.6 MPaG at the outlet of the steam separator 5 and about 0.2 MPaG at the outlet of the capillary 10 during normal operation, the pipe at the subsequent stage of the capillary 10 is connected to the steam separator 5. Even if the blowdown water is introduced above the water level control position 12 and the blowdown water is introduced into the generated water recovery unit 7, the blowdown can be sufficiently performed.

【0020】一方、装置停止時は、水蒸気分離器5、並
びにブローダウン回路の系内の圧力が徐々に低下し大気
圧になる為、細管10後段の立ち上げ配管部14での水
位が水位制御位置と一致した状態で水流が停止して水封
状態となり、ブローダウン水が生成水回収器7に流れな
くなる。よって、従来装置のように電磁遮断弁11がな
くとも、信頼性の高い安定した装置停止が可能となる。
On the other hand, when the apparatus is stopped, the pressure in the steam separator 5 and the blow-down circuit system gradually decreases to atmospheric pressure. The water flow stops in a state where the position coincides with the position, the water seal state is established, and blowdown water does not flow to the generated water recovery unit 7. Therefore, even if the electromagnetic shut-off valve 11 is not provided unlike the conventional apparatus, the apparatus can be stopped stably with high reliability.

【0021】[0021]

【発明の効果】上記のとおり、この発明によれば、冷却
水を通流する冷却板を介装してなる燃料電池本体と、該
冷却板に冷却水を供給し、冷却板から排出される高温の
冷却水を導入して水蒸気と水とに分離する水蒸気分離器
と、燃料電池における生成水を回収するための生成水回
収器とを備え、かつ、前記水蒸気分離器は、内部の貯留
水を生成水回収器へ吐出させるためのブローダウン回路
を備え、このブローダウン回路は、回路の主配管より管
路断面積の小さな細管を用いてなるブローダウン水圧力
調整手段を備えた燃料電池発電装置において、前記生成
水回収器へ吐出するブローダウン水吐出口を、前記水蒸
気分離器における水位制御位置より高い位置に設けたも
のとしたので、装置停止時において水蒸気分離器の貯留
水が全て流出するトラブルを防止し、ブロ−ダウン回路
の簡素化を図って、トータルコストの低減を図ることが
できる。
As described above, according to the present invention, the fuel cell main body having the cooling plate through which the cooling water flows, the cooling water supplied to the cooling plate, and discharged from the cooling plate. A steam separator for introducing high-temperature cooling water to separate into steam and water, and a product water recovery device for recovering product water in the fuel cell, and wherein the steam separator has an internal storage water. A blowdown circuit for discharging water to a generated water recovery unit, the blowdown circuit comprising a blowdown water pressure adjusting means using a narrow pipe having a smaller pipe cross-sectional area than a main pipe of the circuit. In the apparatus, the blowdown water discharge port for discharging to the generated water recovery unit is provided at a position higher than the water level control position in the steam separator, so that all the water stored in the steam separator flows out when the apparatus is stopped. Do To prevent trouble, blow - thereby promoting simplification of the down circuit, it is possible to reduce the total cost.

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

【図1】この発明の実施例に関わる燃料電池発電装置の
システム系統図
FIG. 1 is a system diagram of a fuel cell power generator according to an embodiment of the present invention.

【図2】従来の燃料電池発電装置のシステム系統図FIG. 2 is a system diagram of a conventional fuel cell power generator.

【符号の説明】[Explanation of symbols]

1:燃料電池本体、2:燃料改質器、5:水蒸気分離
器、7:生成水回収器、8:水処理装置、10:細管、
12:水位制御位置、13:吐出口、100:ブローダ
ウン回路。
1: fuel cell main body, 2: fuel reformer, 5: steam separator, 7: produced water collector, 8: water treatment device, 10: thin tube,
12: water level control position, 13: discharge port, 100: blowdown circuit.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 冷却水を通流する冷却板を介装してなる
燃料電池本体と、該冷却板に冷却水を供給し、冷却板か
ら排出される高温の冷却水を導入して水蒸気と水とに分
離する水蒸気分離器と、燃料電池における生成水を回収
するための生成水回収器とを備え、かつ、前記水蒸気分
離器は、内部の貯留水を生成水回収器へ吐出させるため
のブローダウン回路を備え、このブローダウン回路は、
回路の主配管より管路断面積の小さな細管を用いてなる
ブローダウン水圧力調整手段を備えた燃料電池発電装置
において、前記生成水回収器へ吐出するブローダウン水
吐出口を、前記水蒸気分離器における水位制御位置より
高い位置に設けたことを特徴とする燃料電池発電装置。
1. A fuel cell main body including a cooling plate through which cooling water flows, supplying cooling water to the cooling plate, and introducing high-temperature cooling water discharged from the cooling plate to form steam. A steam separator for separating water and a generated water collector for collecting generated water in the fuel cell, and the steam separator is for discharging stored water inside to the generated water collector. A blow-down circuit is provided.
In a fuel cell power generation apparatus provided with a blowdown water pressure adjusting means using a small tube having a smaller pipe cross-sectional area than a main pipe of a circuit, a blowdown water discharge port for discharging to the generated water recovery unit is provided with the steam separator. A fuel cell power generator provided at a position higher than the water level control position in (1).
【請求項2】 請求項1記載の燃料電池発電装置におい
て、前記ブローダウン水圧力調整手段を、前記水位制御
位置より高い位置に設けたことを特徴とする燃料電池発
電装置。
2. The fuel cell power generator according to claim 1, wherein said blowdown water pressure adjusting means is provided at a position higher than said water level control position.
JP2000098486A 2000-03-31 2000-03-31 Fuel cell power generator Expired - Lifetime JP3741257B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000098486A JP3741257B2 (en) 2000-03-31 2000-03-31 Fuel cell power generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000098486A JP3741257B2 (en) 2000-03-31 2000-03-31 Fuel cell power generator

Publications (2)

Publication Number Publication Date
JP2001283884A true JP2001283884A (en) 2001-10-12
JP3741257B2 JP3741257B2 (en) 2006-02-01

Family

ID=18612961

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000098486A Expired - Lifetime JP3741257B2 (en) 2000-03-31 2000-03-31 Fuel cell power generator

Country Status (1)

Country Link
JP (1) JP3741257B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5229329B2 (en) * 2009-01-08 2013-07-03 パナソニック株式会社 Fuel cell system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5229329B2 (en) * 2009-01-08 2013-07-03 パナソニック株式会社 Fuel cell system
US8535837B2 (en) 2009-01-08 2013-09-17 Panasonic Corporation Fuel cell system

Also Published As

Publication number Publication date
JP3741257B2 (en) 2006-02-01

Similar Documents

Publication Publication Date Title
EP1620911B1 (en) Solid oxide fuel cell with selective anode tail gas circulation
US7354566B2 (en) Fuel gas production method and apparatus
EP2240977B1 (en) Water recovery assembly for use in high temperature fuel cell systems
JP2003243020A (en) Fuel cell system
JPH1126003A (en) Power generation stopping method for fuel cell power generating system
JP2000501227A (en) Operating method of high-temperature fuel cell equipment and high-temperature fuel cell equipment
JP2003282114A (en) Stopping method of fuel cell power generating device
JPH03184270A (en) Method for converting fuel into current and device thereof
JP2020105024A (en) Hydrogen generation system, and operation method
JP2002110207A (en) Fuel cell system and operation method therefor
JP2002063922A (en) Fuel cell system and its operation method
JP2001229951A (en) Fuel-cell system for moving object
US7666537B2 (en) Fuel cell system for preventing hydrogen permeable metal layer degradation
JPH09237635A (en) Solid electrolyte fuel cell
JP3741257B2 (en) Fuel cell power generator
CN101150202B (en) Fuel cell system with purging device and method for operating same
JP2002025596A (en) Phosphoric-acid fuel cell power generating facility
JP3890754B2 (en) Phosphoric acid fuel cell power generator
JP2004199977A (en) Fuel cell generator and its operation method
JPS6313277A (en) In-system gas replacement of fuel cell
JP2003288936A (en) Fuel cell power generating system and its operation method
JP4502614B2 (en) Fuel cell system
JPH11233130A (en) Fuel cell power generating facility
JPH0426070A (en) Operation of fuel cell generator
JP2004199878A (en) Fuel cell power generating system

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040322

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20051011

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20051020

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20051102

R150 Certificate of patent or registration of utility model

Ref document number: 3741257

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091118

Year of fee payment: 4

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091118

Year of fee payment: 4

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091118

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101118

Year of fee payment: 5

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111118

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111118

Year of fee payment: 6

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111118

Year of fee payment: 6

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121118

Year of fee payment: 7

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131118

Year of fee payment: 8

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term