JPH09306524A - Water cooled fuel cell power generating system - Google Patents

Water cooled fuel cell power generating system

Info

Publication number
JPH09306524A
JPH09306524A JP8112880A JP11288096A JPH09306524A JP H09306524 A JPH09306524 A JP H09306524A JP 8112880 A JP8112880 A JP 8112880A JP 11288096 A JP11288096 A JP 11288096A JP H09306524 A JPH09306524 A JP H09306524A
Authority
JP
Japan
Prior art keywords
water
fuel cell
copper
mixed
mixed water
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
JP8112880A
Other languages
Japanese (ja)
Inventor
Genichi Ikeda
元一 池田
Tatsuya Ichihashi
達也 市橋
Takashi Ouchi
崇 大内
Harumi Miyama
晴美 深山
Masataka Fujii
優孝 藤井
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
Tokyo Gas Co Ltd
Toho Gas Co Ltd
Original Assignee
Fuji Electric 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, Tokyo Gas Co Ltd, Toho Gas Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP8112880A priority Critical patent/JPH09306524A/en
Publication of JPH09306524A publication Critical patent/JPH09306524A/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 obstruct propagation of microbes in the mixed water, keep stable cooling performance, and reduce the running cost by arranging a sterilizing means generating copper ions in the mixed water in a water treatment system to utilize the sterilization of the copper ion. SOLUTION: A sterilizing means 50 for generating copper ions, arranged in a water treating system 40 constituted with a produced water recovering line 20 and a water treating line 30 is immersed and set in mixed water 28 within a mixed water tank 22, and elutes a copper ion Cu<2+> by reaction with a base or oxygen in the mixed water. The eluted copper ions come ion contact with microbes in a process in which recovered water 29 and tap water are mixed in a fluid state within the mixed water tank 22, and the propagation of microbes in the mixed water is obstructed by the sterilizing action for obstructing a metabolism of the microbe by the sterilization of the copper ion. The clogging of a filter 32 caused by the proliferated microbes is avoided, and the supply of steam for reformation to a fuel reforming device 2 is stabilized.

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、生成水回収系に
水道水により持ち込まれる微生物の増殖を阻止する手段
を備えた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 means for inhibiting the growth of microorganisms brought into tap water in a produced water recovery system.

【0002】[0002]

【従来の技術】図4は従来の水冷式燃料電池発電装置の
要部を示すシステム構成図であり、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190°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,ならびに
必要に応じて設けられる図示しない冷却用の熱交換器1
3などを含む冷却水循環系10が設けられる。
2. Description of the Related Art FIG. 4 is a system configuration diagram showing a main part of a conventional water-cooled fuel cell power generator.
Is a stack of unit cells in which a fuel electrode and an air electrode are arranged with a matrix holding phosphoric acid sandwiched between them, and the fuel gas 2F generated in the fuel reformer 2 is supplied to the fuel electrode,
By supplying air to the air electrode, power generation is performed based on an electrochemical reaction. In addition, the electrochemical reaction of the fuel cell 1 is an exothermic reaction as a whole, and cooling of the fuel cell is necessary to maintain the temperature of the fuel cell 1 at an operating temperature of, for example, about 190 ° C. and perform efficient power generation operation. Will be needed.
Therefore, the fuel cell 1 has a cooling plate 3 that uses pure water as the cooling water 6.
Are laminated, and in order to circulate the cooling water 6 through the cooling plate 3, a steam separator 11 and a circulation pump 12, and a heat exchanger 1 for cooling (not shown) provided as necessary.
A cooling water circulation system 10 including 3 and the like is provided.

【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、原燃料にはエゼクタ4により
水蒸気分離器11で分離した水蒸気の一部が改質用スチ
ームとして混合された状態で燃料改質装置2に供給され
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9を補給する必要があ
る。この純水9には、例えばポンプ31,フィルタ3
2,およびイオン交換式水処理装置33からなる水処理
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29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処理装置33の負荷を軽
くできるので、燃料電池発電装置には、空気オフガス7
中および燃焼排ガス8中に含まれる水蒸気を凝縮し、回
収水29として回収する生成水回収装置21、および回
収水29に水道水を加えた混合水28として貯留する回
収水タンク22からなる生成水回収系20が設けられ、
水処理系30と併せて水処理システム40が構成され
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 as the raw fuel, and a part of the steam separated by the steam separator 11 by the ejector 4 is supplied to the fuel reforming device 2 in a mixed state as reforming steam. Therefore, it is necessary to supply the pure water 9 to the cooling water circulation system 10 in accordance with the amount of steam used for reforming the fuel. The pure water 9 contains, for example, a pump 31 and a filter 3.
2, and ion-exchanged water from which impurities have been removed is used in a water treatment system 30 including an ion-exchange water treatment device 33. However, the water contained in the air off-gas 7 discharged from the air electrode of the fuel cell 1 (power generation) Water) and water contained in the combustion exhaust gas 8 of the burner of the fuel reformer 2 (combustion produced water)
Since the recovered water 29 in which the water is condensed has less impurities than tap water, and the load on the ion exchange type processing device 33 can be lightened accordingly, the air off gas 7
Generated water comprising a generated water recovery device 21 for condensing water vapor contained in the inside and combustion exhaust gas 8 and recovering it as recovered water 29, and a recovered water tank 22 for storing it as a mixed water 28 obtained by adding tap water to the recovered water 29. A recovery system 20 is provided,
A water treatment system 40 is configured together with the water treatment system 30.

【0004】また、混合水タンク22内に貯留した混合
水28の一部はポンプ31を介してフィルタ32,イオ
ン交換式水処理装置33を含む水処理系30に送られ、
不純物を除去した純水9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22の水位の低下は水道水などの補給水系23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 28 stored in the mixed water tank 22 is sent to a water treatment system 30 including a filter 32 and an ion exchange type water treatment device 33 through a pump 31.
Pure water 9 from which impurities have been removed is supplied to the cooling water circulation system 10 to compensate for the shortage of the cooling water 6, and tap water is supplied from a makeup water system 23 such as tap water to reduce the water level in the recovered water tank 22. This maintains a constant water balance.

【0005】[0005]

【発明が解決しようとする課題】前述のように構成され
た従来の水冷式燃料電池発電装置において、燃料電池1
の発電量が大きい高負荷時には、排ガス7および8中に
含まれる水蒸気量が多く、冷却水循環系10および生成
水回収系20の水バランスが保たれ易い。しかしなが
ら、低負荷時など排ガス中の水蒸気量が少ない状態、あ
るいは夏季など生成水回収装置21の冷却水温度が上昇
する状態では、回収水29の量が減少して水バランスが
保てなくなる状態が発生する。そこで、混合水タンク2
2には市水などの水道水の補給水系23が設けられ、回
収水29の不足分を水道水により補充し、混合水28と
して水処理系30に供給し、水バランスを保つ対策が施
される。また、燃料電池発電装置の運転初期には混合水
タンク22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。
In the conventional water-cooled fuel cell power generator having the above-described structure, the fuel cell 1
When the load is large and the load is large, the amount of water vapor contained in the exhaust gases 7 and 8 is large, and the water balance of the cooling water circulation system 10 and the produced water recovery system 20 is easily maintained. However, when the amount of water vapor in the exhaust gas is small, such as when the load is low, or when the temperature of the cooling water of the produced water recovery device 21 rises, such as in summer, the amount of recovered water 29 decreases and the water balance cannot be maintained. appear. Therefore, mixed water tank 2
2 is provided with a makeup water system 23 for tap water such as city water, and the shortage of the recovered water 29 is supplemented with tap water and supplied to the water treatment system 30 as a mixed water 28 to take measures for maintaining water balance. It Further, the mixed water tank 22 is empty at the beginning of the operation of the fuel cell power generator, and the operation is started after the water is first filled with tap water. Also, when the water level in the mixed water tank drops during operation, tap water is replenished.

【0006】これらの水道水は通常塩素殺菌により微生
物(バクテリア)の繁殖が抑制されているが、生存した
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
1を通過して生成水回収装置21に流入する排ガス7お
よび8は無菌状態であり、生成水回収装置21で凝縮し
て得られる回収水29もほぼ無菌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22内の混合水
温度はイオン交換式水処理装置33の許容温度である2
0〜50°C に保持されているため微生物が繁殖し易い
条件が整う場合がある。このため、混合水タンク22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
度的に増殖してフィルタ32で捕捉され、フィルタが培
地となって微生物がさらに繁殖するため、フィルタ32
が閉塞状態となり、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冷却水循環系10内の水バランス
が崩れ、燃料改質装置2や燃料電池1に運転障害が発生
するという問題が発生する。また、フィルタ32の寿命
が極端に短くなり、ろ材を交換するための保守管理が煩
雑化するという問題も発生する。
[0006] These tap waters usually contain a trace amount of surviving bacteria, although the growth of microorganisms (bacteria) is suppressed by chlorine sterilization. On the other hand, the exhaust gases 7 and 8 flowing through the fuel reformer burner in a high temperature atmosphere exceeding 200 ° C and the fuel cell 1 and flowing into the produced water recovery device 21 are in a sterile state and are condensed in the produced water recovery device 21. The recovered water 29 obtained as a result is also maintained in a substantially sterile state and has no sterilizing ability. Furthermore, the temperature of the mixed water in the mixed water tank 22 is the allowable temperature of the ion exchange type water treatment device 33.
Since the temperature is maintained at 0 to 50 ° C, there are cases where conditions under which microorganisms can easily propagate are set. For this reason, the microorganisms in the tap water replenished in the mixed water tank 22 are acceleratedly proliferated in the recovered water tank and are captured by the filter 32, and the filter serves as a medium to further propagate the microorganisms.
Is blocked, and due to this, the supply of pure water to the water vapor separator 11 is insufficient, the water balance in the cooling water circulation system 10 is lost, and an operation failure occurs in the fuel reformer 2 and the fuel cell 1. Occurs. In addition, the service life of the filter 32 becomes extremely short, and maintenance and management for replacing the filter medium becomes complicated.

【0007】また、一旦回収水タンク内に多量に増殖し
た微生物の除去方法としては、薬液洗浄が知られている
が、水処理システムの構成材料が主にSUS製であるた
めに塩素系薬品の注入は好ましくなく、薬注後十分な純
水洗浄を必要とするために燃料電池発電装置の停止期間
が長引くとともに、その保守作業が煩雑化するため、結
果的に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。さらに、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
境を再び作ってしまうという問題も発生する。
[0007] Chemical solution cleaning is known as a method for removing microorganisms that have once grown in large quantities in the recovered water tank. However, since the constituent materials of the water treatment system are mainly made of SUS, chlorine-based chemicals are used. Injecting is not preferable, and the maintenance period of the fuel cell power generator is prolonged because of the need for sufficient deionized water cleaning after chemical injection, and the maintenance work is complicated, resulting in the running cost of the fuel cell power generator. There is a problem of causing rise in Further, there is a problem that the environment for the growth of microorganisms is recreated by refilling with tap water after completion of the cleaning work.

【0008】この発明の課題は、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。
An object of the present invention is to eliminate the need for complicated maintenance work such as cleaning chemicals in a produced water recovery system and a 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により冷却される
とともに、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する生成水回収装置、および回
収水に水道水を添加した混合水として貯留する混合水タ
ンクからなる生成水回収系と、前記混合水を純水に変換
して前記冷却水循環系に供給する水処理系とからなる水
処理システムを備えた水冷式燃料電池発電装置におい
て、銅イオンを発生する滅菌手段を前記水処理システム
内の混合水中に設ける。
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 into the cooling water, and a generated water recovery device that condenses and recovers water vapor in the exhaust gas of the fuel cell and the fuel reformer, and a mixed water obtained by adding tap water to the recovered water. In a water-cooled fuel cell power generator comprising a water treatment system including a produced water recovery system including a mixed water tank that stores the water as a water supply and a water treatment system that converts the mixed water into pure water and supplies the pure water to the cooling water circulation system. A sterilizing means for generating copper ions is provided in the mixed water in the water treatment system.

【0010】ここで、請求項2に記載の発明は、請求項
1に記載の水冷式燃料電池発電装置において、滅菌手段
を混合水タンク内に設けられた銅製部材とすると良い。
また、請求項3に記載の発明は、請求項2に記載の水冷
式燃料電池発電装置において、銅製部材を混合水タンク
内に設けられた銅網で構成すると良い。さらに、請求項
4に記載の発明は、請求項2に記載の水冷式燃料電池発
電装置において、銅製部材を混合水タンク内に設けられ
た筒状の銅網と、この筒状の銅網内に充填されたラッシ
ヒ・リング状の銅材片とで構成すると好便である。
According to the second aspect of the present invention, in the water-cooled fuel cell power generator according to the first aspect, the sterilizing means may be a copper member provided in the mixed water tank.
Further, in the invention described in claim 3, in the water-cooled fuel cell power generator according to claim 2, the copper member may be configured by a copper net provided in the mixed water tank. Further, the invention according to claim 4 is, in the water-cooled fuel cell power generator according to claim 2, a tubular copper net provided with a copper member in a mixed water tank, and the inside of the tubular copper net. It is convenient to construct it with a Raschig-ring-shaped copper material piece filled in.

【0011】請求項1に記載の発明では、混合水中に設
けた滅菌手段から発生する銅イオンの毒性により微生物
の物質代謝が妨げられるので、水道水によって水処理シ
ステム内に持ち込まれた微生物の増殖が、薬液洗浄など
の方法によらずに阻止される。ここで、請求項2に記載
の発明では、銅製部材が混合水中の塩基や酸素との反応
によって徐々に溶け、銅イオン(Cu2+)の発生源とし
て機能する滅菌手段が形成される。
According to the first aspect of the present invention, the toxicity of copper ions generated from the sterilizing means provided in the mixed water hinders the substance metabolism of the microorganisms. Therefore, the growth of the microorganisms brought into the water treatment system by tap water is increased. However, it is blocked regardless of a method such as chemical cleaning. Here, in the invention described in claim 2, the copper member is gradually dissolved by the reaction with the base and oxygen in the mixed water to form a sterilizing means that functions as a generation source of copper ions (Cu 2+ ).

【0012】また、請求項3に記載の発明では、銅製部
材を混合水タンク内に設けられた銅網としたことによ
り、混合水タンク内での水の流動による回収水と水道水
の混合を妨げることなく、かつ少ない銅材量で広い銅イ
オンの溶出表面積を確保できる滅菌手段が形成される。
さらに、請求項4に記載の発明では、筒状の銅網内にラ
ッシヒ・リング状の銅材片を充填したことにより、ラッ
シヒ・リング状の銅材片の充填量によって銅イオン溶出
表面積の制御,言い換えれば銅イオン濃度の制御が容易
になり、銅イオン濃度が高く、滅菌作用に優れた滅菌手
段が容易に形成される。
Further, in the invention according to claim 3, since the copper member is a copper net provided in the mixed water tank, the recovered water and the tap water are mixed by the water flow in the mixed water tank. A sterilizing means that can secure a wide elution surface area of copper ions with a small amount of copper material without hindering is formed.
Further, in the invention according to claim 4, by filling the Raschig ring-shaped copper material pieces in the tubular copper net, the copper ion elution surface area is controlled by the filling amount of the Raschig ring-shaped copper material pieces. In other words, the control of the copper ion concentration is facilitated, the copper ion concentration is high, and a sterilizing means excellent in sterilization action is easily formed.

【0013】[0013]

【発明の実施の形態】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は請求項1または請求項2に記載の発明の水冷
式燃料電池発電装置の一実施例を簡略化して示すシステ
ム構成図である。図において、生成水回収系20と水処
理系30とで構成される水処理システム40内に設けら
れて銅イオンを発生する滅菌手段50は、この実施例で
は銅製部材からなり、生成水回収系20の混合水タンク
22内に混合水28に浸漬した状態で設けられ、混合水
中の塩基や酸素と反応して銅イオン(Cu2+)を溶出す
る。溶出した銅イオンは、混合水タンク22内で回収水
29と水道水とが流動状態で混合する過程で微生物と接
触し、銅イオンの毒性によって微生物の物質代謝を阻害
する滅菌作用により、混合水中の微生物の増殖が阻止さ
れる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on embodiments. 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 system configuration diagram schematically showing one embodiment of the water-cooled fuel cell power generator of the invention described in claim 1 or 2. In the figure, a sterilizing means 50 for generating copper ions, which is provided in a water treatment system 40 composed of a produced water recovery system 20 and a water treatment system 30, is made of a copper member in this embodiment, and the produced water recovery system is used. It is provided in a mixed water tank 22 of 20 so as to be immersed in the mixed water 28, and reacts with a base and oxygen in the mixed water to elute copper ions (Cu 2+ ). The eluted copper ions come into contact with microorganisms in the process of mixing the recovered water 29 and tap water in the mixed water tank 22 in a fluidized state, and due to the sterilizing action of inhibiting the substance metabolism of the microorganisms due to the toxicity of copper ions, the mixed water is mixed. The growth of microorganisms of

【0014】したがって、混合水タンク22から水処理
系30に供給される混合水28に含まれる微生物の量は
極めて少なく、フィルタ32で捕捉された微生物がフィ
ルタ32が培地となってさらに繁殖してフィルタ32が
閉塞状態となる事態が回避され、冷却水循環系10への
純水9の安定供給により冷却水循環系10内の水バラン
スが保持され、燃料電池1の冷却性能および燃料改質装
置2への改質用スチームの供給を安定化できる利点が得
られる。また、フィルタ32のろ材の交換頻度が減少
し、これに伴って保守作業が簡素化されるので、燃料電
池発電装置のランニング・コストの低減効果が得られ
る。さらに、長期間使用することにより銅製部材の表面
が不純物層で覆われて銅イオンの溶出量が低下した場合
には、新たな銅製部材を混合タンク22内に追加投入す
るか、新たな銅製部材に差し替えることによって滅菌作
用を回復できるので、混合水タンク22や混合水配管,
フィルタ,等の薬液洗浄を必要とせず、したがって燃料
電池発電装置の運転停止時間を短縮し、保守作業を一層
簡素化し、さらにランニング・コストを低減できる利点
が得られる。
Therefore, the amount of microorganisms contained in the mixed water 28 supplied to the water treatment system 30 from the mixed water tank 22 is extremely small, and the microorganisms captured by the filter 32 further propagate as the medium of the filter 32. The situation in which the filter 32 is blocked is avoided, the stable supply of the pure water 9 to the cooling water circulation system 10 maintains the water balance in the cooling water circulation system 10, and the cooling performance of the fuel cell 1 and the fuel reformer 2 The advantage of being able to stabilize the supply of the reforming steam is obtained. Further, since the frequency of replacement of the filter medium of the filter 32 is reduced and the maintenance work is simplified accordingly, the running cost of the fuel cell power generator can be reduced. Furthermore, when the surface of the copper member is covered with an impurity layer due to long-term use and the elution amount of copper ions is reduced, a new copper member is additionally charged into the mixing tank 22, or a new copper member is added. The sterilization effect can be restored by replacing the
Since there is no need to clean the liquid chemicals such as filters, it is possible to shorten the operation stop time of the fuel cell power generator, further simplify the maintenance work, and further reduce the running cost.

【0015】図2は請求項3に記載の燃料電池発電装置
の一実施例を示す要部の断面図であり、銅製部材からな
る滅菌手段51を銅網とした点が前述の実施例と異なっ
ている。この実施例の場合、滅菌手段51を混合水タン
ク22内に同軸状に配置された複数の筒状の銅網で構成
することにより、混合水タンク22内での水の流動によ
る回収水と水道水の混合を妨げることなく、かつ少ない
銅材量で広い銅イオンの溶出表面積が確保される。
FIG. 2 is a sectional view of an essential part showing an embodiment of the fuel cell power generator according to claim 3, which is different from the above embodiment in that the sterilizing means 51 made of a copper member is a copper net. ing. In the case of this embodiment, the sterilizing means 51 is composed of a plurality of cylindrical copper nets coaxially arranged in the mixed water tank 22, so that the recovered water and the tap water due to the flow of water in the mixed water tank 22 are provided. A wide elution surface area of copper ions can be secured with a small amount of copper material without hindering the mixing of water.

【0016】銅イオン(Cu2+ )の毒性は微生物の種類
や接触時間により致死濃度および忍耐濃度が異なること
が知られている。また、銅網から溶出する銅イオンの濃
度は混合水の水質や温度の影響を受けて変化する。した
がって、混合水タンク22内に設ける銅網の量は燃料電
池発電装置の設置場所での上記諸条件を考慮した実験に
より求めるしかない。しかしながら、滅菌手段51を銅
網としたことにより、筒状の銅網の重ね枚数やメッシュ
により銅網の投入量の調整が容易であり、最適致死濃度
の銅イオンを溶出可能な滅菌手段51を容易に形成でき
る利点が得られる。
It is known that the toxicity of copper ion (Cu 2+ ) differs in lethal concentration and patience concentration depending on the type of microorganism and contact time. Moreover, the concentration of copper ions eluted from the copper net changes under the influence of the water quality and temperature of the mixed water. Therefore, the amount of the copper net provided in the mixed water tank 22 can only be obtained by an experiment in consideration of the above conditions at the installation location of the fuel cell power generator. However, since the sterilizing means 51 is a copper net, it is easy to adjust the input amount of the copper net by the number of stacked copper nets and the mesh, and the sterilizing means 51 capable of eluting copper ions of the optimum lethal concentration is provided. The advantage is that it can be easily formed.

【0017】図3は請求項4に記載の発明の一実施例を
示す要部の断面図であり、この実施例が図2に示す実施
例と異なるところは、滅菌手段52が、複数の筒状の銅
網53と、複数の筒状の銅網53内に充填されたラッシ
ヒ・チューブ状の銅材片54との複合体として構成され
た点にある。この実施例によれば、ラッシヒ・チューブ
状の銅材片54により、少ない銅量で広い溶出表面積を
確保できるので、ことに高い致死濃度を必要とする滅菌
手段を容易に形成できる利点が得られる。
FIG. 3 is a sectional view of an essential part showing an embodiment of the invention described in claim 4. This embodiment differs from the embodiment shown in FIG. 2 in that the sterilizing means 52 has a plurality of cylinders. The point is that it is configured as a composite of a copper mesh 53 in the shape of a cylinder and a copper material piece 54 in the shape of a Raschig tube filled in the plurality of cylindrical copper meshes 53. According to this embodiment, since the Raschig tube-shaped copper material piece 54 can secure a large elution surface area with a small amount of copper, there is an advantage that a sterilizing means requiring a particularly high lethal concentration can be easily formed. .

【0018】[0018]

【発明の効果】この発明は前述のように、銅イオンを発
生する滅菌手段を水処理システム内の混合水中に設ける
よう構成した。その結果、銅イオンの毒性を利用して混
合水中の微生物の増殖を薬液洗浄によらずに阻止できる
ので、従来技術で問題になった増殖した微生物によるフ
ィルタの閉塞と、これによる冷却水循環系の水バランス
の崩れが排除され、燃料電池発電装置の安定した冷却性
能および改質反応水の供給性能が保持されるとともに、
フィルタのろ材の交換頻度が低減され、燃料電池発電装
置の保守管理費およびランニング・コストの低減にも貢
献できる利点が得られる。
As described above, the present invention is constructed such that the sterilizing means for generating copper ions is provided in the mixed water in the water treatment system. As a result, the toxicity of copper ions can be used to prevent the growth of microorganisms in the mixed water without the need for chemical cleaning.Therefore, clogging of the filter by the grown microorganisms, which was a problem in the prior art, and the cooling water circulation system Disturbance of water balance is eliminated, stable cooling performance of the fuel cell power generator and reforming reaction water supply performance are maintained, and
The frequency of replacing the filter medium of the filter is reduced, and the advantage that it can contribute to the reduction of the maintenance cost and the running cost of the fuel cell power generator is obtained.

【0019】また、滅菌手段を銅網,ラッシヒ・リング
状の銅材片等の銅製部材として混合水タンク内に設ける
よう構成すれば、微生物の滅菌に必要な致死濃度の銅イ
オンが少ない銅材量で容易に得られるとともに、運転を
停止せずに銅製部材を追加,更新できる利便性が得られ
る。
If the sterilizing means is provided in the mixed water tank as a copper member such as a copper net or a Raschig ring-shaped copper material piece, the copper material with a small lethal concentration of copper ions necessary for sterilization of microorganisms can be obtained. The amount can be easily obtained, and the convenience that the copper member can be added or updated without stopping the operation is obtained.

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

【図1】請求項1または請求項2に記載の発明の水冷式
燃料電池発電装置の一実施例を簡略化して示すシステム
構成図
FIG. 1 is a system configuration diagram showing in simplified form one embodiment of a water-cooled fuel cell power generator of the invention according to claim 1 or claim 2.

【図2】請求項3に記載の燃料電池発電装置の一実施例
を示す要部の断面図
FIG. 2 is a cross-sectional view of a main part showing an embodiment of the fuel cell power generator according to claim 3;

【図3】請求項4に記載の発明の一実施例を示す要部の
断面図
FIG. 3 is a sectional view of an essential part showing an embodiment of the invention described in claim 4;

【図4】従来の水冷式燃料電池発電装置の要部を示すシ
ステム構成図
FIG. 4 is a system 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、7・・・空気オフガス、8・・
・燃焼排ガス、9・・・純水、10・・・冷却水循環
系、11・・・水蒸気分離器、12・・・循環ポンプ、
13・・・冷却用熱交換器、14・・・エゼクタ、20
・・・生成水回収系、21・・・生成水回収装置、22
・・・混合水タンク、23・・・補給水系、28・・・
混合水、29・・・回収水、30・・・水処理系、31
・・・ポンプ、32・・・フィルタ、33・・・イオン
交式水処理装置、40・・・水処理システム、50・・
・滅菌手段(銅製部材)、51・・・滅菌手段(銅
網)、52・・・滅菌手段(銅網+ラッシヒ・チューブ
状の銅材片)。
1 ... Fuel cell, 2 ... Fuel reformer, 3 ... Cooling plate, 6 ... Cooling water, 7 ... Air off-gas, 8 ...
・ Combustion exhaust gas, 9 ... Pure water, 10 ... Cooling water circulation system, 11 ... Water vapor separator, 12 ... Circulation pump,
13 ... Cooling heat exchanger, 14 ... Ejector, 20
... Generated water recovery system, 21 ... Generated water recovery device, 22
... Mixed water tank, 23 ... Makeup water system, 28 ...
Mixed water, 29 ... Recovered water, 30 ... Water treatment system, 31
... Pump, 32 ... Filter, 33 ... Ion exchange water treatment device, 40 ... Water treatment system, 50 ...
-Sterilizing means (copper member), 51 ... Sterilizing means (copper net), 52 ... Sterilizing means (copper net + Raschig tube-shaped copper material piece).

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/50 540 C02F 1/50 540E 550 550B (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 (72)発明者 大内 崇 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 深山 晴美 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 藤井 優孝 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 (51) Int.Cl. 6 Identification code Internal reference number FI Technical indication location C02F 1/50 540 C02F 1/50 540E 550 550B (72) Inventor Tatsuya Ichihashi Minato-ku, Nagoya, Aichi 1-27, Kanagawa-cho (72) Takashi Ouchi 1-1, Tanabe Nitta, Kawasaki-ku, Kawasaki-shi, Kanagawa Prefecture Fuji Electric Co., Ltd. (72) Harumi Miyama 1, Nitta Tanabe, Kawasaki-ku, Kanagawa-ken No. 1 in Fuji Electric Co., Ltd. (72) Inventor, Yutaka Fujii 1-1, Tanabe Nitta, Kawasaki-ku, Kawasaki-shi, Kanagawa 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
する冷却水循環系により冷却されるとともに、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
回収する生成水回収装置、および回収水に水道水を添加
した混合水として貯留する混合水タンクからなる生成水
回収系と、前記混合水を純水に変換して前記冷却水循環
系に供給する水処理系とからなる水処理システムを備え
た水冷式燃料電池発電装置において、銅イオンを発生す
る滅菌手段を前記水処理システム内の混合水中に設けた
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 is cooled by a cooling water circulation system that circulates cooling water through a cooling pipe of the cooling plate, and the fuel cell and the fuel reformer are also provided. Generated water recovery device that condenses and recovers water vapor in the exhaust gas of the device, and a generated water recovery system that consists of a mixed water tank that stores the mixed water with tap water added to the recovered water, and converts the mixed water into pure water In a water-cooled fuel cell power generator equipped with a water treatment system comprising a water treatment system for supplying to the cooling water circulation system, sterilizing means for generating copper ions is provided in the mixed water in the water treatment system. A water-cooled fuel cell power generator featuring.
【請求項2】請求項1に記載の水冷式燃料電池発電装置
において、滅菌手段が混合水タンク内に設けられた銅製
部材であ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 sterilizing means is a copper member provided in the mixed water tank.
【請求項3】請求項2に記載の水冷式燃料電池発電装置
において、銅製部材が混合水タンク内に設けられた銅網
である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 2, wherein the copper member is a copper net provided in the mixed water tank.
【請求項4】請求項2に記載の水冷式燃料電池発電装置
において、銅製部材が混合水タンク内に設けられた筒状
の銅網と、この筒状の銅網内に充填されたラッシヒ・リ
ング状の銅材片とからなる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 2, wherein a copper member is provided with a tubular copper net in the mixed water tank, and a Raschig battery filled in the tubular copper net. A water-cooled fuel cell power generation device comprising a ring-shaped piece of copper material.
JP8112880A 1996-05-08 1996-05-08 Water cooled fuel cell power generating system Pending JPH09306524A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8112880A JPH09306524A (en) 1996-05-08 1996-05-08 Water cooled fuel cell power generating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8112880A JPH09306524A (en) 1996-05-08 1996-05-08 Water cooled fuel cell power generating system

Publications (1)

Publication Number Publication Date
JPH09306524A true JPH09306524A (en) 1997-11-28

Family

ID=14597846

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8112880A Pending JPH09306524A (en) 1996-05-08 1996-05-08 Water cooled fuel cell power generating system

Country Status (1)

Country Link
JP (1) JPH09306524A (en)

Cited By (7)

* 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
WO2005074064A1 (en) * 2004-01-30 2005-08-11 Matsushita Electric Industrial 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
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
JP2012028159A (en) * 2010-07-23 2012-02-09 Panasonic Corp Fuel cell system
CN110822778A (en) * 2019-11-27 2020-02-21 四川川润液压润滑设备有限公司 Multi-path pressure flow constant water cooling system for test platform and application method thereof

Cited By (11)

* 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
US7981555B2 (en) 2002-07-30 2011-07-19 Panasonic Corporation Method of operating a fuel cell system
WO2005074064A1 (en) * 2004-01-30 2005-08-11 Matsushita Electric Industrial Co., Ltd. Fuel cell system
CN100423342C (en) * 2004-01-30 2008-10-01 松下电器产业株式会社 Fuel cell system
US7763388B2 (en) 2004-01-30 2010-07-27 Panasonic Corporation 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
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
JP2012028159A (en) * 2010-07-23 2012-02-09 Panasonic Corp Fuel cell system
CN110822778A (en) * 2019-11-27 2020-02-21 四川川润液压润滑设备有限公司 Multi-path pressure flow constant water cooling system for test platform and application method thereof

Similar Documents

Publication Publication Date Title
US6461487B1 (en) Generation and delivery device for ozone gas
CN1239750C (en) Water electrolyzing device
US20100219066A1 (en) Water electrolysis system
CN105355950B (en) A kind of macro-organism cathode microbial fuel cell stack device
WO1998042617A2 (en) An integrated ozone generator system
JPH09306523A (en) Water cooled fuel cell power generating system
JPH09306524A (en) Water cooled fuel cell power generating system
WO2012120835A1 (en) Energy system
CN208071821U (en) A kind of ozonization purifier with heating function
US20050211567A1 (en) Apparatus and method for integrated hypochlorite and hydrogen fuel production and electrochemical power generation
JP2001232394A (en) Water treatment equipment for fuel cell
JP5353034B2 (en) Fuel cell power generator
JPH0963611A (en) Water-cooled fuel cell power generating apparatus
JPH0963612A (en) Water-cooled fuel cell power generating apparatus
JP2001236981A (en) Water treatment system for fuel cell generator
JP2009081084A (en) Fuel cell power generation apparatus
JP4662277B2 (en) Electrodeionization equipment
JP5093437B2 (en) Bacteria control method for fuel cell system
JP3132627B2 (en) Water recovery system for fuel cell power plant
JP3240981B2 (en) Electrolytic ozone generator
JP5286851B2 (en) Fuel cell power generator
JP2021016813A (en) Oxygen gas supply apparatus and sewage treatment system
KR102609121B1 (en) Fuel cell system with electrodeionization device
KR101980067B1 (en) A liquid electrolyte fuel cell system
JP2003249255A (en) Fuel cell system