JPH0963611A - Water-cooled fuel cell power generating apparatus - Google Patents

Water-cooled fuel cell power generating apparatus

Info

Publication number
JPH0963611A
JPH0963611A JP7210304A JP21030495A JPH0963611A JP H0963611 A JPH0963611 A JP H0963611A JP 7210304 A JP7210304 A JP 7210304A JP 21030495 A JP21030495 A JP 21030495A JP H0963611 A JPH0963611 A JP H0963611A
Authority
JP
Japan
Prior art keywords
water
fuel cell
cooling
mixed
cell power
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
JP7210304A
Other languages
Japanese (ja)
Inventor
Genichi Ikeda
元一 池田
Nobuhiro Iwasa
信弘 岩佐
Tatsuya Ichihashi
達也 市橋
Haruki Matsuda
治樹 松田
Takashi Murakami
隆 村上
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
Osaka Gas Co Ltd
Tokyo Gas Co Ltd
Toho Gas Co Ltd
Original Assignee
Fuji Electric Co Ltd
Osaka Gas Co Ltd
Tokyo Gas Co Ltd
Toho 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 Fuji Electric Co Ltd, Osaka Gas Co Ltd, Tokyo Gas Co Ltd, Toho Gas Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP7210304A priority Critical patent/JPH0963611A/en
Publication of JPH0963611A publication Critical patent/JPH0963611A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a water-cooled fuel cell power generating apparatus in which microbe propagation can be prevented without requiring complicated maintenance work such as washing of a produced water recovering system and a water treating system with chemicals. SOLUTION: A fuel cell 1 consisting of layered bodies of a plurality of unit cells and cooling plates 3 is provided with a cooling water circulating system 10 to circulate cooling water 6 to cooling pipes in the cooling plates, a produced water recovering system 20 which condenses steam in waste gases 7, 8 of the fuel cell and a fuel reforming apparatus 2 to recover as water, mixes the water with tap water to give mixed water 26, and store the mixed water 26, and a water treating system 30 which converts the mixed water into pure water 26P and supplies to the cooling water circulating system 10. As an antibacterial filter 40 to inhibit propagation of microbes in the mixed water 26, tanks 41, 42 filled with granular adsorbents bearing antibacterial metal films on the surface are installed in an upper stream side of a mixed water circulating system 25 in the produced water recovering system or of an ion-exchange type pure water producing apparatus 31 in the water treating system 30.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、冷却水循環系統,冷
却水補給装置を備えた水冷式燃料電池発電装置、ことに
細菌の増殖を防止した冷却水補給装置を有する水冷式燃
料電池発電装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water-cooled fuel cell power generator equipped with a cooling water circulation system and a cooling water replenishing device, and more particularly to a water cooling fuel cell power generator having a cooling water replenishing device preventing bacterial growth. .

【0002】[0002]

【従来の技術】図2は従来の水冷式燃料電池発電装置の
要部を示す構成図であり、りん酸形燃料電池1はりん酸
を保持するマトリックスを挟んで燃料電極および空気電
極を配した単位セルの積層体からなり、燃料電極に燃料
改質装置2で生成した燃料ガス2Fを供給し,空気電極
に空気を供給することにより、電気化学反応に基づいて
発電が行われる。また、燃料電池1の電気化学反応は全
体として発熱反応であり、燃料電池1の温度を例えば1
90°C 程度の運転温度に保持して効率の良い発電運転
を行うためには燃料電池の冷却が必要になる。そこで、
燃料電池1には純水を冷却水6とする冷却板3が積層さ
れ、この冷却板3に冷却水6を循環するために、水蒸気
分離器11および循環ポンプ12,および必要に応じて
設けられる図示しない冷却用の熱交換器などを含む冷却
水循環系統10が連結される。
2. Description of the Related Art FIG. 2 is a block diagram showing a main part of a conventional water-cooled fuel cell power generator. In a phosphoric acid fuel cell 1, a fuel electrode and an air electrode are arranged with a matrix holding phosphoric acid interposed therebetween. It is composed of a stack of unit cells, and the fuel gas 2F generated by the fuel reforming device 2 is supplied to the fuel electrode and the air is supplied to the air electrode, so that power generation is performed based on the electrochemical reaction. Moreover, the electrochemical reaction of the fuel cell 1 is an exothermic reaction as a whole, and the temperature of the fuel cell 1 is
The fuel cell must be cooled in order to perform efficient power generation operation while maintaining the operating temperature at about 90 ° C. Therefore,
A cooling plate 3 having pure water as cooling water 6 is laminated on the fuel cell 1. In order to circulate the cooling water 6 through the cooling plate 3, a water vapor separator 11 and a circulation pump 12 and, if necessary, are provided. A cooling water circulation system 10 including a heat exchanger for cooling (not shown) and the like is connected.

【0003】原燃料を水素リッチな燃料ガスに改質する
ためには、原燃料としてのメタンガス等に改質用スチー
ムを加えて水とメタンとの反応を触媒で促進して行う燃
料改質装置2が用いられ、改質用スチームには水蒸気分
離器12で分離した水蒸気の一部が利用される。したが
って、冷却水循環系統10には燃料の改質に使用した水
蒸気量に対応して純水6Pを補給する必要がある。この
純水6Pにはイオン交換式の純水装置31およびポンプ
32を含む水処理系統30で不純物を除去したイオン交
換水が用いられるが、燃料電池1の空気電極から排出さ
れる空気オフガス7中に含まれる水分(発電生成水)や
燃料改質装置2のバーナの燃焼排ガス8中に含まれる水
分(燃焼生成水)を凝縮した回収水を用いた方が水道水
よりも不純物が少なく、その分イオン交換式の純水装置
の負荷を軽くできるので、燃料電池発電装置には生成水
回収系統20と水処理系統30とで構成される冷却水補
給装置が付加される。
In order to reform a raw fuel into a hydrogen-rich fuel gas, a fuel reformer for adding a reforming steam to methane gas or the like as a raw fuel to promote a reaction between water and methane with a catalyst. 2 is used, and a part of the steam separated by the steam separator 12 is used for the reforming steam. Therefore, it is necessary to supply the pure water 6P to the cooling water circulation system 10 in accordance with the amount of steam used for reforming the fuel. For this pure water 6P, ion-exchanged water from which impurities have been removed in a water treatment system 30 including an ion-exchange type pure water device 31 and a pump 32 is used. In the air-off gas 7 discharged from the air electrode of the fuel cell 1. The amount of impurities contained in the recovered water, which is obtained by condensing the water contained in the water (generated water generated) and the water contained in the combustion exhaust gas 8 of the burner of the fuel reformer 2 (combustion generated water) has less impurities than tap water. Since the load of the ion-exchange type deionized water device can be reduced, a cooling water replenishing device including a produced water recovery system 20 and a water treatment system 30 is added to the fuel cell power generation device.

【0004】生成水回収系統20は、例えば直接式熱交
換器部および回収水タンク部を内包した生成水回収塔2
1と、回収水タンク中の回収水に水道水を加えた混合水
26を循環ポンプ22,冷却用の熱交換器23,および
ノズル24を介して直接式熱交換器の上方から散布する
混合水循環系25とで構成され、ノズルから散布される
混合水と空気オフガス7,燃焼排ガス8とが向流接触し
て生成水が回収される。
The produced water recovery system 20 is, for example, a produced water recovery tower 2 including a direct heat exchanger section and a recovered water tank section.
1 and a mixed water circulation in which the mixed water 26 obtained by adding tap water to the recovered water in the recovered water tank is sprayed from above the direct heat exchanger through the circulation pump 22, the heat exchanger 23 for cooling, and the nozzle 24. The mixed water sprayed from the nozzle and the air off gas 7 and the combustion exhaust gas 8 come into countercurrent contact with each other to collect the produced water.

【0005】また、生成水回収塔21内に貯留した混合
水26の一部はポンプ22を介してイオン交換式の純水
装置31を含む水処理系統30に送られ、不純物を除去
した純水として冷却水循環系統10に供給されて冷却水
6の不足分を補償するとともに、回収水タンクの水位の
低下は図示しない水道水供給系から水道水を供給するこ
とにより一定水位の水バランスが保持される。
A part of the mixed water 26 stored in the produced water recovery tower 21 is sent to a water treatment system 30 including an ion-exchange type deionized water device 31 via a pump 22 to remove impurities from the deionized water. Is supplied to the cooling water circulation system 10 to compensate for the shortage of the cooling water 6, and the decrease in the water level of the recovered water tank is maintained by supplying tap water from a tap water supply system (not shown) to maintain a constant water level. It

【0006】[0006]

【発明が解決しようとする課題】従来の生成水回収系統
20において、運転初期には生成水回収塔21内の混合
水タンクは空状態であり、先ず水道水による水張りを行
った後運転が開始される。また、運転中に混合水タンク
内の水位が低下した場合にも水道水の補給が行われる。
これらの水道水は通常塩素殺菌により微生物の繁殖が抑
制されているが、不純物として微量のバクテリア等を含
んでいる。一方、200°C を越える高温雰囲気の燃料
改質器バーナ,および燃料電池を通過して生成水回収塔
21に流入するオフガス7および8は無菌状態であり、
生成水回収塔で凝縮して得られる回収水もほぼ純水状態
に保持されるため殺菌能力がない。さらに、混合水タン
ク内の混合水温度は通常40〜60°C に保持されてい
るため微生物が繁殖し易い条件になる。このため、生成
水回収塔内に補給された水道水中の微生物が回収水タン
ク内で加速度的に増殖し、これがポンプ22によりイオ
ン交換式純水装置31に送り込まれて捕捉されるため、
イオン交換式純水装置31が閉塞状態になり、これが原
因で水蒸気分離器11への純水の補給が不足して水バラ
ンスが崩れ、燃料改質装置2や燃料電池1に運転障害が
発生するとともに、イオン交換式純水装置31の保守間
隔が極端に短くなって保守の煩雑化を招くという問題が
発生する。
In the conventional produced water recovery system 20, the mixed water tank in the produced water recovery tower 21 is empty at the beginning of the operation, and the operation is started after the water is first filled with tap water. To be done. Also, when the water level in the mixed water tank drops during operation, tap water is replenished.
These tap waters usually have microbial sterilization suppressed by chlorine sterilization, but contain trace amounts of bacteria as impurities. On the other hand, the off-gas 7 and 8 flowing through the fuel reformer burner in a high temperature atmosphere exceeding 200 ° C. and the fuel cell and flowing into the produced water recovery tower 21 are aseptic,
The recovered water obtained by condensing in the generated water recovery tower is also kept in a substantially pure water state and has no sterilizing ability. Furthermore, since the temperature of the mixed water in the mixed water tank is usually maintained at 40 to 60 ° C, it becomes a condition that microorganisms can easily propagate. Therefore, the microorganisms in the tap water replenished in the produced water recovery tower proliferate at an accelerated rate in the recovered water tank, and this is sent to the ion exchange type deionized water device 31 by the pump 22 and captured.
The ion exchange type pure water device 31 is in a closed state, and due to this, the pure water supply to the water vapor separator 11 is insufficient, the water balance is lost, and an operation failure occurs in the fuel reformer 2 and the fuel cell 1. At the same time, there arises a problem that the maintenance interval of the ion exchange type pure water device 31 becomes extremely short and the maintenance becomes complicated.

【0007】また、一旦回収水タンク内に多量に増殖し
た微生物は薬液洗浄などにより除去するしかなく、その
実施に際しては燃料電池の運転を一時停止し、燃料電池
1や燃料改質器2に連通する配管を遮断した状態で薬剤
を注入して一定時間循環または放置して殺菌を行った
後、水道水で洗浄しつつ系外に排出される洗浄水のpH
を監視し、中和を確認した上で水道水による水張りを行
うという煩雑な操作が必要であり、保守作業が煩雑化し
て燃料電池発電装置のランニングコストの上昇を招くと
いう問題がある。また、洗浄作業の終了後再び水道水に
よる水張りを行うことにより、微生物の増殖環境を作っ
てしまうという問題がある。
[0007] In addition, the microorganisms that have once grown in a large amount in the recovered water tank have to be removed by chemical cleaning or the like. In that case, the operation of the fuel cell is temporarily stopped and the fuel cell 1 and the fuel reformer 2 are connected. The pH of the washing water discharged outside the system while washing with tap water after sterilizing by injecting chemicals with the pipes blocked and circulating or standing for a certain period of time.
It is necessary to perform a complicated operation of monitoring the temperature and confirming neutralization before filling water with tap water, and there is a problem that maintenance work becomes complicated and the running cost of the fuel cell power generator increases. In addition, there is a problem in that a microbial growth environment is created by performing water filling with tap water again after the cleaning work is completed.

【0008】この発明の目的は、生成水回収系統や水処
理系統の薬剤洗浄などの煩雑な保守作業を必要とせず、
微生物の繁殖を防止できる水冷式燃料電池発電装置を提
供することにある。
The object of the present invention is to eliminate the need for complicated maintenance work such as cleaning chemicals in the produced water recovery system and the water treatment system,
An object of the present invention is to provide a water-cooled fuel cell power generator that can prevent the growth of microorganisms.

【0009】[0009]

【課題を解決するための手段】前述の目的を達成するた
めに、請求項1に記載の発明は、複数の単位セルと冷却
板との積層体からなる燃料電池が、前記冷却板の冷却パ
イプに冷却水を循環する冷却水循環系統と、前記燃料電
池および燃料改質装置の排ガス中の水蒸気を凝縮して回
収し水道水を添加した混合水として貯留する生成水回収
系統,および前記混合水を純水に変換して前記冷却水循
環系統に供給する水処理系統からなる冷却水補給装置と
を備えた水冷式燃料電池発電装置において、前記混合水
中の微生物の増殖を阻止する抗菌性フィルターを備え
る。
In order to achieve the above-mentioned object, the invention according to claim 1 provides a fuel cell comprising a laminate of a plurality of unit cells and cooling plates, and a cooling pipe for the cooling plates. A cooling water circulation system that circulates cooling water, a produced water recovery system that condenses and recovers water vapor in the exhaust gas of the fuel cell and the fuel reformer, and stores it as mixed water to which tap water is added, and the mixed water. A water-cooled fuel cell power generator including a cooling water replenishing device including a water treatment system that converts the water into pure water and supplies the cooling water circulation system with an antibacterial filter that prevents the growth of microorganisms in the mixed water.

【0010】ここで、請求項2に記載の発明は、抗菌性
フィルターとして、表面に抗菌性金属膜を添着した粒状
吸着剤の充填槽を用いると良い。また、請求項3に記載
の発明は、生成水回収系統に設けられて排ガスと混合水
を向流接触させる混合水循環系に抗菌性フィルターを設
けると良い。さらに、請求項4に記載の発明は、水処理
系統の上流側に抗菌性フィルターを設けると良い。
Here, in the invention as set forth in claim 2, it is preferable to use, as the antibacterial filter, a granular adsorbent filling tank having an antibacterial metal film attached to the surface thereof. Further, in the invention according to claim 3, it is preferable that an antibacterial filter is provided in the mixed water circulation system which is provided in the produced water recovery system and makes the exhaust gas and the mixed water countercurrently contact. Further, in the invention according to claim 4, an antibacterial filter may be provided on the upstream side of the water treatment system.

【0011】[0011]

【作用】請求項1に記載の発明では、混合水が抗菌性フ
ィルターを通過する際、混合水中の微生物がフィルター
に補足されるとともに、フィルターの抗菌性によりその
繁殖が阻止されるので、回収水に水道水を混合すること
により生成水回収系統に持ち込まれる微生物の捕捉およ
び増殖の抑制が可能になり、したがって、イオン交換式
純水装置の閉塞障害が排除され、イオン交換樹脂の交換
インターバルの延長により、冷却水循環系統に純水が長
時間安定供給される。
In the invention described in claim 1, when the mixed water passes through the antibacterial filter, microorganisms in the mixed water are captured by the filter, and the antibacterial property of the filter prevents the growth of the recovered water. By mixing tap water with the water, it is possible to capture and suppress the growth of microorganisms brought into the produced water recovery system, thus eliminating the blockage obstacle of the ion exchange type pure water device and extending the exchange interval of the ion exchange resin. As a result, pure water is stably supplied to the cooling water circulation system for a long time.

【0012】ここで、請求項2に記載の発明では、抗菌
性フィルターに表面に抗菌性金属膜を添着した抗菌性吸
着剤の充填槽を用いたことにより、粒状吸着剤が混合水
中の微生物をその吸着力により捕捉すると同時に、抗菌
性金属膜がその抗菌性により捕捉した微生物の増殖を阻
止するので、抗菌性フィルターを通過した混合水はその
微生物量が低減される。
According to the second aspect of the present invention, since the antibacterial filter is provided with the antibacterial adsorbent filling tank having the antibacterial metal film attached to the surface thereof, the granular adsorbent absorbs the microorganisms in the mixed water. At the same time as being captured by the adsorptive power, the antibacterial metal film inhibits the growth of microorganisms captured by the antibacterial property, so that the amount of the microorganisms in the mixed water that has passed through the antibacterial filter is reduced.

【0013】また、請求項3に記載の発明では、生成水
回収系統に設けられて排ガスと混合水を向流接触させる
混合水循環系に抗菌性フィルターを設けたことにより、
生成水回収塔内に貯留された混合水が抗菌性フィルター
を通って繰り返しろ過されるので、運転中水道水の補給
によって生成水回収塔内に侵入する微生物の蓄積および
繁殖が阻止され、微生物量が低減された混合水が水処理
系統に安定して供給される。
According to the third aspect of the present invention, the antibacterial filter is provided in the mixed water circulation system which is provided in the produced water recovery system to bring the exhaust gas and the mixed water into countercurrent contact.
Since the mixed water stored in the generated water recovery tower is repeatedly filtered through the antibacterial filter, the accumulation and propagation of microorganisms that enter the generated water recovery tower are stopped by the supply of tap water during operation, and the amount of microorganisms The mixed water with reduced water is stably supplied to the water treatment system.

【0014】さらに、請求項4に記載の発明では、水処
理系統の上流側に抗菌性フィルターを設けたことによ
り、イオン交換式純水装置の直前で混合水中の細菌量を
低減できることになり、イオン交換樹脂の閉塞障害をよ
り効果的に排除し、その保守間隔の更なる延長が可能に
なる。
Further, in the invention according to claim 4, since the antibacterial filter is provided on the upstream side of the water treatment system, the amount of bacteria in the mixed water can be reduced immediately before the ion exchange type deionized water device. The blocking obstacle of the ion exchange resin can be eliminated more effectively, and the maintenance interval can be further extended.

【0015】[0015]

【実施例】以下この発明を実施例に基づいて説明する。
なお、従来例と同じ参照符号を付けた部材は従来例のそ
れと同じ機能をもつので、その説明を省略する。図1は
この発明の水冷式燃料電池発電装置の一実施例を示す簡
略化したシステム構成図である。図において、実施例で
は生成水回収系統20の混合水循環系25に抗菌性フィ
ルター41を設けるとともに、水処理系統30の純水装
置31の上流側にも抗菌性フィルター42を設けた。2
つの抗菌性フィルター40としては、粒状吸着剤として
の活性炭の表面に銀,銅などの抗菌性金属を活性炭の吸
着力を大幅に阻害しない範囲で添着した抗菌性活性炭の
充填槽を用いた。
EXAMPLES The present invention will be described below based on examples.
Since the members having the same reference numerals as those of the conventional example have the same functions as those of the conventional example, the description thereof will be omitted. FIG. 1 is a simplified system configuration diagram showing an embodiment of a water-cooled fuel cell power generator of the present invention. In the figure, in the embodiment, an antibacterial filter 41 is provided in the mixed water circulation system 25 of the produced water recovery system 20, and an antibacterial filter 42 is also provided upstream of the pure water device 31 of the water treatment system 30. Two
As one antibacterial filter 40, an antibacterial activated carbon filling tank was used in which an antibacterial metal such as silver or copper was impregnated on the surface of activated carbon as a granular adsorbent within a range that did not significantly impair the adsorptive power of the activated carbon.

【0016】実施例では、生成水回収塔21内に貯留さ
れた混合水26が抗菌性フィルター41を通って繰り返
しろ過されるので、水張り時に侵入した微生物はもとよ
り、運転中水道水の補給によって生成水回収塔内に侵入
する微生物も、粒状活性炭の吸着力により捕捉されると
同時に、抗菌性金属膜がその抗菌性によって捕捉した微
生物の増殖を阻止するので、抗菌性フィルターを通過し
た混合水はその微生物量が徐々に低減され、微生物量が
低減された混合水26が水処理系統30に安定して供給
される。
In the embodiment, since the mixed water 26 stored in the produced water recovery tower 21 is repeatedly filtered through the antibacterial filter 41, it is produced not only by the microorganisms invading at the time of water filling but also by supplying tap water during operation. Microorganisms that enter the water recovery tower are also captured by the adsorptive power of the granular activated carbon, and at the same time, the antibacterial metal membrane blocks the growth of the microorganisms that are captured due to their antibacterial properties, so the mixed water that has passed through the antibacterial filter is The amount of microorganisms is gradually reduced, and the mixed water 26 in which the amount of microorganisms is reduced is stably supplied to the water treatment system 30.

【0017】また、水処理系統30に供給された混合水
は抗菌性フィルター42により再び微生物がろ過される
とともに、混合水に含まれる他の不純物の吸着ろ過も行
われるので、イオン交換式純水装置31に供給される混
合水はその微生物量および不純物量が大幅に低減された
状態となり、高度に浄化された純水26Pが冷却水循環
系10に補給される。その結果、従来例において生成水
回収塔21内で加速度的に増殖した微生物により、イオ
ン交換式純水装置31が閉塞状態になり、これが原因で
水蒸気分離器11への純水の補給が不足して水バランス
が崩れ、燃料改質装置2や燃料電池1に運転障害が発生
するという事態が回避され、イオン交換式純水装置31
の保守間隔が従来例に比べて大幅に延長された。また、
生成水回収塔21の薬液洗浄も、抗菌性フィルターの抗
菌性活性炭を定期的に交換することによって不要にな
り、保守作業が省力化されて運転コストの低減効果が得
られるとともに、薬液洗浄を行うために必要とした燃料
電池発電装置の運転停止も回避できることになり、燃料
電池発電装置の長期連続運転を可能にする利点が得られ
る。
In addition, the mixed water supplied to the water treatment system 30 is filtered by the antibacterial filter 42 again for microorganisms, and adsorption filtration of other impurities contained in the mixed water is also performed. The mixed water supplied to the device 31 is in a state in which the amount of microorganisms and the amount of impurities are significantly reduced, and highly purified pure water 26P is replenished to the cooling water circulation system 10. As a result, in the conventional example, the ion-exchange type deionized water device 31 is closed due to the microorganisms that have acceleratedly grown in the produced water recovery tower 21, which causes insufficient supply of deionized water to the water vapor separator 11. As a result, a situation in which the water balance is lost and an operation failure occurs in the fuel reforming device 2 and the fuel cell 1 is avoided.
The maintenance interval was significantly extended compared to the conventional example. Also,
The chemical cleaning of the generated water recovery tower 21 is also unnecessary by regularly exchanging the antibacterial activated carbon of the antibacterial filter, the maintenance work is labor-saving, the operating cost is reduced, and the chemical cleaning is performed. Therefore, it is possible to avoid the operation stop of the fuel cell power generator, which is necessary, and there is an advantage that the long-term continuous operation of the fuel cell power generator can be achieved.

【0018】なお、抗菌性フィルター41,42をいず
れか一方に絞って設置するよう構成し、装置を簡素化て
も良い。また、抗菌性フィルター40を互いに切替え可
能な2つの並列充填槽で構成すれば、抗菌性活性炭を定
期的に交換する作業を燃料電池発電装置の運転を停止せ
ずに行える利点が得られる。
The antibacterial filters 41 and 42 may be arranged so as to be narrowed down to one of them to simplify the apparatus. Further, if the antibacterial filter 40 is composed of two parallel filling tanks that can be switched to each other, there is an advantage that the operation of periodically exchanging the antibacterial activated carbon can be performed without stopping the operation of the fuel cell power generator.

【0019】[0019]

【発明の効果】この発明の水冷式燃料電池発電装置は前
述のように、生成水回収系統に水道水を補給することに
より混合水中に侵入する微生物を、例えば抗菌性活性炭
の充填槽などからなる抗菌性フィルターを設けて捕捉か
つその増殖を抑制するよう構成した。その結果、増殖し
た微生物によってイオン交換式純水装置が閉塞し、冷却
水循環系への純水の補給が困難になるなどのトラブルが
回避されて燃料電池発電装置の長期連続運転が可能にな
るとともに、イオン交換樹脂の交換間隔の延長,および
煩雑な薬液洗浄などの保守作業の排除によって運転コス
トも低減されるので、燃料電池発電装置の運転停止や煩
雑な保守作業を必要とせずに各水系統の微生物の増殖を
抑制できる、低運転コストで長期信頼性の高い水冷式燃
料電池発電装置を提供することができる。
As described above, the water-cooled fuel cell power generator according to the present invention is composed of, for example, a filling tank of antibacterial activated carbon for the microorganisms that enter the mixed water by supplying the generated water recovery system with tap water. An antibacterial filter was provided to capture and suppress its proliferation. As a result, the grown microorganisms block the ion exchange type deionized water device, and troubles such as difficulty in replenishing deionized water to the cooling water circulation system are avoided and a long-term continuous operation of the fuel cell power generation device becomes possible. The operating cost is also reduced by extending the ion-exchange resin replacement interval and eliminating maintenance work such as complicated chemical cleaning, so each water system can be operated without the need to shut down the fuel cell power generator or perform any complicated maintenance work. It is possible to provide a water-cooled fuel cell power generation device that can suppress the growth of microorganisms, and that has a low operating cost and high long-term reliability.

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

【図1】この発明の水冷式燃料電池発電装置の一実施例
を示す簡略化したシステム構成図
FIG. 1 is a simplified system configuration diagram showing an embodiment of a water-cooled fuel cell power generator of the present invention.

【図2】従来の水冷式燃料電池発電装置の要部を示す構
成図
FIG. 2 is a configuration diagram showing a main part of a conventional water-cooled fuel cell power generator.

【符号の説明】[Explanation of symbols]

1 燃料電池 2 燃料改質装置 3 冷却板 6 冷却水 6P 純水 7 空気オフガス 8 燃焼排ガス 10 冷却水循環系統 11 水蒸気分離器 12 ポンプ 20 生成水回収系統 21 生成水回収塔 22 ポンプ 23 熱交換器 24 ノズル 25 混合水循環系 26 混合水 26P 純水 30 水処理系統 31 イオン交換式純水装置 32 ポンプ 40 抗菌性フィルター(41,42) 1 Fuel Cell 2 Fuel Reforming Device 3 Cooling Plate 6 Cooling Water 6P Pure Water 7 Air Off-gas 8 Combustion Exhaust Gas 10 Cooling Water Circulation System 11 Steam Separator 12 Pump 20 Generated Water Recovery System 21 Generated Water Recovery Tower 22 Pump 23 Heat Exchanger 24 Nozzle 25 Mixed water circulation system 26 Mixed water 26P Pure water 30 Water treatment system 31 Ion exchange type pure water device 32 Pump 40 Antibacterial filter (41, 42)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 池田 元一 神奈川県逗子市久木2丁目6番B9号 (72)発明者 岩佐 信弘 大阪府岸和田市葛城町910番55号 (72)発明者 市橋 達也 愛知県名古屋市港区金川町1丁目27番、金 川社宅A−106号 (72)発明者 松田 治樹 神奈川県川崎市川崎区田辺新田1番1号 富士電機株式会社内 (72)発明者 村上 隆 神奈川県川崎市川崎区田辺新田1番1号 富士電機株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Motoichi Ikeda 2-6 B9, Hisagi, Zushi City, Kanagawa Prefecture (72) Nobuhiro Iwasa 910-55, Katsuragi Town, Kishiwada City, Osaka Prefecture (72) Inventor Tatsuya Ichihashi 1-27 Kanagawa-cho, Minato-ku, Nagoya-shi, Aichi Prefecture, A-106, Kanagawa company housing (72) Inventor Haruki Matsuda 1-1, Tanabe Nitta, Kawasaki-ku, Kawasaki-shi, Kanagawa Fuji Electric Co., Ltd. (72) Inventor Takashi Murakami 1-1, Tanabe Nitta, Kawasaki-ku, Kawasaki-shi, Kanagawa Prefecture Fuji Electric Co., Ltd.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】複数の単位セルと冷却板との積層体からな
る燃料電池が、前記冷却板の冷却パイプに冷却水を循環
する冷却水循環系統と、前記燃料電池および燃料改質装
置の排ガス中の水蒸気を凝縮して回収し水道水を添加し
た混合水として貯留する生成水回収系統、および前記混
合水を純水に変換して前記冷却水循環系統に供給する水
処理系統からなる冷却水補給装置とを備えた水冷式燃料
電池発電装置において、前記混合水中の微生物の増殖を
阻止する抗菌性フィルターを備えたことを特徴とする水
冷式燃料電池発電装置。
1. A fuel cell comprising a stack of a plurality of unit cells and a cooling plate, a cooling water circulation system for circulating cooling water in a cooling pipe of the cooling plate, and exhaust gas of the fuel cell and the fuel reformer. Cooling water replenishing device comprising a generated water recovery system for condensing and recovering the above water vapor and storing it as mixed water to which tap water has been added, and a water treatment system for converting the mixed water into pure water and supplying it to the cooling water circulation system A water-cooled fuel cell power generator comprising: a water-cooled fuel cell power generator including an antibacterial filter for inhibiting the growth of microorganisms in the mixed water.
【請求項2】請求項1記載の水冷式燃料電池発電装置に
おいて、抗菌性フィルターが表面に抗菌性金属膜を添着
した粒状吸着剤の充填槽からなることを特徴とする水冷
式燃料電池発電装置。
2. The water-cooled fuel cell power generator according to claim 1, wherein the antibacterial filter comprises a granular adsorbent filling tank having an antibacterial metal film attached to the surface thereof. .
【請求項3】請求項1記載の水冷式燃料電池発電装置に
おいて、生成水回収系統に設けられて排ガスと混合水を
向流接触させる混合水循環系に抗菌性フィルターを設け
たことを特徴とする水冷式燃料電池発電装置。
3. The water-cooled fuel cell power generator according to claim 1, wherein an antibacterial filter is provided in the mixed water circulation system which is provided in the produced water recovery system and makes the exhaust gas and the mixed water come into countercurrent contact. Water-cooled fuel cell power generator.
【請求項4】請求項1記載の水冷式燃料電池発電装置に
おいて、水処理系統の上流側に抗菌性フィルターを設け
たことを特徴とする水冷式燃料電池発電装置。
4. The water-cooled fuel cell power generator according to claim 1, further comprising an antibacterial filter provided upstream of the water treatment system.
JP7210304A 1995-08-18 1995-08-18 Water-cooled fuel cell power generating apparatus Pending JPH0963611A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7210304A JPH0963611A (en) 1995-08-18 1995-08-18 Water-cooled fuel cell power generating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7210304A JPH0963611A (en) 1995-08-18 1995-08-18 Water-cooled fuel cell power generating apparatus

Publications (1)

Publication Number Publication Date
JPH0963611A true JPH0963611A (en) 1997-03-07

Family

ID=16587196

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7210304A Pending JPH0963611A (en) 1995-08-18 1995-08-18 Water-cooled fuel cell power generating apparatus

Country Status (1)

Country Link
JP (1) JPH0963611A (en)

Cited By (8)

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WO2004012292A1 (en) * 2002-07-30 2004-02-05 Matsushita Electric Industrial Co., Ltd. Fuel cell generation apparatus
JP2005108561A (en) * 2003-09-29 2005-04-21 Toyota Motor Corp Fuel cell system
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WO2006088053A1 (en) * 2005-02-18 2006-08-24 Matsushita Electric Industrial Co., Ltd. Fuel cell system and method of operating the same
JP2008135271A (en) * 2006-11-28 2008-06-12 Kyocera Corp Fuel cell device
US7763388B2 (en) 2004-01-30 2010-07-27 Panasonic Corporation Fuel cell system
JP2010238413A (en) * 2009-03-30 2010-10-21 Aisin Seiki Co Ltd Fuel cell system
JP2010257737A (en) * 2009-04-24 2010-11-11 Aisin Seiki Co Ltd Fuel cell system

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004012292A1 (en) * 2002-07-30 2004-02-05 Matsushita Electric Industrial Co., Ltd. Fuel cell generation apparatus
EP1503444A1 (en) * 2002-07-30 2005-02-02 Matsushita Electric Industrial Co., Ltd. Fuel cell generation apparatus
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US7981555B2 (en) 2002-07-30 2011-07-19 Panasonic Corporation Method of operating a fuel cell system
JP2005108561A (en) * 2003-09-29 2005-04-21 Toyota Motor Corp Fuel cell system
US7763388B2 (en) 2004-01-30 2010-07-27 Panasonic Corporation Fuel cell system
JP2005276621A (en) * 2004-03-25 2005-10-06 Aisin Seiki Co Ltd Fuel cell system
WO2006088053A1 (en) * 2005-02-18 2006-08-24 Matsushita Electric Industrial Co., Ltd. Fuel cell system and method of operating the same
US8445158B2 (en) 2005-02-18 2013-05-21 Panasonic Corporation Fuel cell system and operation method thereof
JP2008135271A (en) * 2006-11-28 2008-06-12 Kyocera Corp Fuel cell device
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JP2010257737A (en) * 2009-04-24 2010-11-11 Aisin Seiki Co Ltd Fuel cell system

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