JP3280164B2 - Steam condensed water circulation device for fuel cell power generator and control method thereof - Google Patents

Steam condensed water circulation device for fuel cell power generator and control method thereof

Info

Publication number
JP3280164B2
JP3280164B2 JP18795694A JP18795694A JP3280164B2 JP 3280164 B2 JP3280164 B2 JP 3280164B2 JP 18795694 A JP18795694 A JP 18795694A JP 18795694 A JP18795694 A JP 18795694A JP 3280164 B2 JP3280164 B2 JP 3280164B2
Authority
JP
Japan
Prior art keywords
condensed water
steam
flow rate
fuel cell
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.)
Expired - Fee Related
Application number
JP18795694A
Other languages
Japanese (ja)
Other versions
JPH0850907A (en
Inventor
康幹 久保田
雄治 澤田
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
Osaka Gas Co Ltd
Original Assignee
Fuji Electric Co Ltd
Osaka Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd, Osaka Gas Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP18795694A priority Critical patent/JP3280164B2/en
Publication of JPH0850907A publication Critical patent/JPH0850907A/en
Application granted granted Critical
Publication of JP3280164B2 publication Critical patent/JP3280164B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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

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、燃料電池本体で生じ
た蒸気から熱を回収し凝縮させて再度燃料電池本体へ冷
却水として循環させる燃料電池発電装置の蒸気凝縮水循
環装置とその制御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam condensed water circulating apparatus for a fuel cell power generator for recovering heat from steam generated in a fuel cell main body, condensing the same, and circulating it again as cooling water to the fuel cell main body, and a control method therefor. .

【0002】[0002]

【従来の技術】燃料電池発電装置では、燃料電池本体に
冷却水を供給して、電気化学反応による発電にともなっ
て生ずる発熱を蒸気として外部に取り出し、有効に熱利
用するとともに、蒸気を凝縮させて再度燃料電池本体の
冷却水として用いる方法が一般的に採られている。
2. Description of the Related Art In a fuel cell power generator, cooling water is supplied to a fuel cell main body, and heat generated due to power generation by an electrochemical reaction is taken out as steam to effectively utilize the heat and condense the steam. In general, a method of using the cooling water again for the fuel cell main body is adopted.

【0003】図2は、燃料電池発電装置の従来の代表的
な蒸気凝縮水循環装置を表す基本系統図である。図にお
いて、燃料電池本体1はモデル的に表示されており、図
示されていない電解質層を燃料極2と空気極3とで挟持
した単セルを、冷却板4を適宜挿入しながら積層するこ
とにより構成されている。冷却板4を通流して燃料電池
本体1の発熱を除去するための冷却水は、循環ポンプ9
によって水蒸気分離器5から冷却水供給流路7を介して
供給される。冷却板4を通流して燃料電池本体1の発熱
により高温となった蒸気は冷却水排出流路8を介して再
び水蒸気分離器5へと戻される。
FIG. 2 is a basic system diagram showing a conventional typical steam condensed water circulation device of a fuel cell power generation device. In the figure, a fuel cell main body 1 is shown as a model, and a single cell in which an electrolyte layer (not shown) is sandwiched between a fuel electrode 2 and an air electrode 3 is laminated by appropriately inserting a cooling plate 4. It is configured. Cooling water for removing heat generated by the fuel cell body 1 through the cooling plate 4 is supplied to a circulation pump 9.
Is supplied from the steam separator 5 through the cooling water supply channel 7. The steam that has flowed through the cooling plate 4 and has been heated by the heat generated by the fuel cell main body 1 is returned to the steam separator 5 again through the cooling water discharge passage 8.

【0004】水蒸気分離器5の圧力は、圧力調整弁10
によって蒸気を熱回収装置31へと放出することによっ
て調節される。熱回収装置31においては、送られてき
た高温の蒸気を例えば外部から送られる冷却水と熱交換
させる等の方法によって、外部へと熱を回収し、これに
対応して蒸気が冷却される。冷却された蒸気の凝縮水は
凝縮水タンク32に溜められる。凝縮水タンク32に貯
液された凝縮水の液面が所定のレベルの範囲になると凝
縮水ポンプ33がオン−オフ制御され、貯液量が多くな
ると凝縮水は水蒸気分離器5へと戻される。なお、凝縮
水ポンプ33から水蒸気分離器5へ至る経路に設けられ
た手動弁15は通常の運転においては常時開放状態にあ
り、また制御弁14は、特に図示していないが水蒸気分
離器5の液面が所定値より高くなると閉止される弁であ
り通常は開放状態にある。したがって、凝縮水タンク3
2から水蒸気分離器5へ送られる凝縮水の量は凝縮水ポ
ンプ33のオン−オフにより支配されている。
The pressure of the steam separator 5 is controlled by a pressure regulating valve 10.
To release heat to the heat recovery device 31. The heat recovery device 31 recovers heat to the outside by, for example, exchanging heat of the sent high-temperature steam with cooling water sent from the outside, and correspondingly cools the steam. The condensed water of the cooled steam is stored in the condensed water tank 32. When the level of the condensed water stored in the condensed water tank 32 falls within a predetermined level range, the condensed water pump 33 is turned on and off. When the stored amount increases, the condensed water is returned to the steam separator 5. . The manual valve 15 provided in the path from the condensed water pump 33 to the steam separator 5 is normally open during normal operation, and the control valve 14 is connected to the steam separator 5 (not shown). This valve is closed when the liquid level becomes higher than a predetermined value, and is normally in an open state. Therefore, the condensed water tank 3
The amount of condensed water sent from 2 to the steam separator 5 is controlled by the on / off of the condensed water pump 33.

【0005】補給水タンク21、補給水供給ポンプ2
2、水処理装置23ならびに補給水制御弁24で構成さ
れる系統は、水蒸気分離器5の貯水量が不足した場合に
補給水を供給する系統であり、水蒸気分離器5に付設の
液面計20により検知された信号により補給水制御弁2
4を開閉制御している。
[0005] Makeup water tank 21, makeup water supply pump 2
2. The system composed of the water treatment device 23 and the make-up water control valve 24 is a system that supplies make-up water when the amount of water stored in the steam separator 5 is insufficient, and a level gauge attached to the steam separator 5. 20 according to the signal detected by the control valve 20
4 is controlled to open and close.

【0006】[0006]

【発明が解決しようとする課題】上述のように、従来の
燃料電池発電装置では、燃料電池本体へ送られた冷却水
が加熱されて生じた蒸気を熱回収設備に送り熱を有効に
回収し、さらにこれを水蒸気分離器に戻して冷却水とし
て再循環させる効率的な蒸気凝縮水循環装置が構成され
ている。
As described above, in the conventional fuel cell power generator, the steam generated by heating the cooling water sent to the fuel cell body is sent to a heat recovery facility to effectively recover the heat. Further, an efficient steam condensed water circulating apparatus for returning the steam to the steam separator and recirculating it as cooling water is constituted.

【0007】しかしながら、本構成による蒸気凝縮水循
環装置にあっても、凝縮水タンクに貯えられた凝縮水の
水蒸気分離器への供給が凝縮水ポンプの運転をオン−オ
フ制御することにより行われているために、水蒸気分離
器での発生蒸気量が大きく変動する難点がある。すなわ
ち、凝縮水の温度は水蒸気分離器の温度に比べて本質的
に低いので、凝縮水ポンプが運転されて凝縮水が水蒸気
分離器へ供給されると、水蒸気分離器の温度が下がり発
生蒸気量が低下する。一方、凝縮水ポンプが停止すると
温度の低い凝縮水の供給がなくなるので、水蒸気分離器
の温度は相対的に上がり発生蒸気量が増加する。このよ
うに水蒸気分離器での発生蒸気量が大きく変動すると、
熱回収設備へ送られる流量が大きく変動し、装置の安定
した運転が困難となる。さらに複数台の燃料電池発電装
置によって1台の熱回収設備を運転する場合にあって
は、各燃料電池発電装置からの発生蒸気量が上記のよう
に大きく変動すると熱回収設備の運転が困難で、熱回収
設備に凝縮水流量の制御装置を設置せざるを得ない等の
問題がある。
However, even in the steam condensed water circulating apparatus according to this configuration, the supply of the condensed water stored in the condensed water tank to the steam separator is performed by controlling the operation of the condensed water pump on and off. Therefore, there is a problem that the amount of steam generated in the steam separator fluctuates greatly. That is, since the temperature of the condensed water is essentially lower than the temperature of the steam separator, when the condensed water pump is operated and the condensed water is supplied to the steam separator, the temperature of the steam separator falls and the amount of generated steam is reduced. Decrease. On the other hand, when the condensed water pump is stopped, the supply of low-temperature condensed water is stopped, so that the temperature of the steam separator rises relatively and the amount of generated steam increases. When the amount of steam generated in the steam separator fluctuates greatly,
The flow rate sent to the heat recovery equipment fluctuates greatly, making stable operation of the apparatus difficult. Further, when one heat recovery facility is operated by a plurality of fuel cell power generators, it is difficult to operate the heat recovery facility if the amount of steam generated from each fuel cell power generator fluctuates greatly as described above. In addition, there is a problem that a condensed water flow control device must be installed in the heat recovery equipment.

【0008】また、上記の従来の構成では、すべての凝
縮水を再び水蒸気分離器に戻し再循環させる効率的な運
転方法をとっているが、長期にわたり継続して連続使用
すると、系統に残留する汚れによって水質が徐々に劣化
し、燃料電池発電装置の特性が低下するという問題点が
あった。また、この方式では、循環する系統全体が清浄
であることが必須条件であり、運転に際しては熱回収設
備をはじめ構成する機器部品を事前に試運転し清浄化し
ておくことが必要であった。
Further, in the above-described conventional configuration, an efficient operation method is employed in which all the condensed water is returned to the steam separator and recirculated. However, if the condensed water is continuously used for a long time, the condensed water remains in the system. There has been a problem that the water quality gradually deteriorates due to the contamination, and the characteristics of the fuel cell power generator deteriorate. Further, in this system, it is an essential condition that the entire circulating system is clean, and during operation, it is necessary to perform a trial operation and clean the equipment components including the heat recovery equipment in advance.

【0009】この発明は上記のごとき背景のもとになさ
れたもので、その目的は、(1) 燃料電池発電装置の水蒸
気分離器からの発生蒸気量をほぼ一定に制御し、熱回収
設備が安定して運転できる蒸気凝縮水循環装置とその制
御方法を提供すること。また、(2) 燃料電池発電装置の
水蒸気分離器の冷却水の水質を一定のレベルを満たすよ
うに制御し、長期にわたり安定した発電特性を可能とす
る蒸気凝縮水循環装置とその制御方法を提供することに
ある。
The present invention has been made on the basis of the above background, and has the following objects. (1) The amount of steam generated from a steam separator of a fuel cell power generation device is controlled to be substantially constant, and heat recovery equipment is provided. An object of the present invention is to provide a steam condensed water circulation device that can be operated stably and a control method thereof. (2) To provide a steam condensate circulating apparatus and a control method thereof, which control the quality of cooling water of a steam separator of a fuel cell power generation apparatus so as to satisfy a certain level and enable stable power generation characteristics over a long period of time. It is in.

【0010】[0010]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明においては、 (1) 燃料電池本体へ冷却水を供給し、かつ冷却後の蒸気
を導入する水蒸気分離器と、水蒸気分離器の蒸気を導入
して熱を取り出す熱回収設備と、熱回収設備で凝縮した
水を貯える凝縮水タンクと、凝縮水タンクの凝縮水を前
記水蒸気分離器に再び戻す凝縮水ポンプとを有する燃料
電池発電装置の蒸気凝縮水循環装置において、前記水蒸
気分離器から前記熱回収設備へ送られる蒸気の流量測定
手段と、前記凝縮水タンクから前記水蒸気分離器へ送ら
れる凝縮水の流量測定手段と、凝縮水タンクから水蒸気
分離器への配管系に組み込まれ、上記の二つの流量測定
手段により検知された流量信号により制御される凝縮水
の流量調整弁とを備えることとする。
In order to achieve the above object, the present invention provides: (1) a steam separator for supplying cooling water to a fuel cell body and introducing steam after cooling; It has a heat recovery facility that introduces steam from the separator to extract heat, a condensed water tank that stores water condensed in the heat recovery facility, and a condensed water pump that returns condensed water in the condensed water tank to the steam separator again. In the steam condensed water circulation device of the fuel cell power generator, a flow rate measuring means of the steam sent from the steam separator to the heat recovery equipment, a flow rate measuring means of the condensed water sent from the condensed water tank to the steam separator, A flow control valve for condensed water, which is incorporated in a piping system from the condensed water tank to the steam separator and is controlled by a flow signal detected by the two flow measuring means, is provided.

【0011】(2) また、上記の蒸気凝縮水循環装置にお
いて、凝縮水タンクから前記の凝縮水の流量調整弁に至
る配管に、少なくとも水処理装置を介して前記水蒸気分
離器へと連結される、開閉弁を付設した分岐配管を設け
ることとする。
(2) In the above-mentioned steam condensed water circulating apparatus, a pipe from the condensed water tank to the condensed water flow control valve is connected to the steam separator via at least a water treatment device. A branch pipe with an on-off valve will be provided.

【0012】[0012]

【作用】上記のように燃料電池発電装置の蒸気凝縮水循
環装置を構成すれば、 (1) 通常の運転に際しては、蒸気流量測定手段と凝縮水
流量測定手段とにより検知された二つの流量信号によ
り、蒸気流量と凝縮水流量が同一となるように凝縮水の
流量調整弁の弁開度を制御することとすれば、従来のオ
ン−オフ制御の場合と異なり、水蒸気分離器へ凝縮水が
定常的に供給されるので、水蒸気分離器の温度変動は微
小に抑えられ、ほぼ一定した蒸気流量が熱回収設備へと
送られ、同様にほぼ一定した凝縮水流量が水蒸気分離器
へ供給されることとなる。したがって熱回収設備を安定
して運転することができる。なお、水処理装置を介して
水蒸気分離器へと連結する分岐配管を設けた場合にあっ
ては、この分岐配管の開閉弁を閉鎖して前記のように凝
縮水の流量調整弁の弁開度を制御すれば同一の作用が得
られる。
[Operation] If the steam condensed water circulation device of the fuel cell power generator is configured as described above, (1) During normal operation, two flow signals detected by the steam flow measuring means and the condensed water flow measuring means are used. By controlling the valve opening of the condensed water flow control valve so that the steam flow rate and the condensed water flow rate are the same, unlike the conventional on-off control, the condensed water flows to the steam separator in a steady state. Temperature fluctuations of the steam separator are suppressed to a very small level, an almost constant steam flow rate is sent to the heat recovery equipment, and an almost constant condensate flow rate is similarly supplied to the steam separator. Becomes Therefore, the heat recovery equipment can be operated stably. In the case where a branch pipe connected to the steam separator via the water treatment device is provided, the on-off valve of the branch pipe is closed and the valve opening of the condensed water flow control valve is closed as described above. The same effect can be obtained by controlling.

【0013】(2) また、かなり長期の運転に伴い凝縮水
の水質が劣化し燃料電池本体の冷却水として不十分とな
った場合には、分岐配管の開閉弁を開放し、かつ蒸気流
量測定手段と凝縮水流量測定手段とにより検知された二
つの流量信号により、凝縮水流量が蒸気流量の一定割合
となるように凝縮水の流量調整弁の弁開度を制御するこ
ととすれば、その他の凝縮水は分岐配管を通って補給水
タンクに至り水処理装置を通って清浄化された後水蒸気
分離器へ供給されることとなり、冷却水は全体として清
浄化が進み水質が向上する。したがって本方式を適宜用
いることにより燃料電池本体の冷却水として十分な水質
を保持することができる。
(2) When the quality of the condensed water deteriorates due to the operation for a considerably long period of time and becomes insufficient as cooling water for the fuel cell body, the on-off valve of the branch pipe is opened and the steam flow rate is measured. If the flow rate of the condensed water is controlled so that the flow rate of the condensed water becomes a constant ratio of the steam flow rate by the two flow rate signals detected by the means and the condensed water flow rate measuring means, The condensed water passes through a branch pipe, reaches a makeup water tank, is purified through a water treatment device, is supplied to a steam separator, and the cooling water is entirely purified and the water quality is improved. Therefore, by appropriately using this method, it is possible to maintain sufficient water quality as cooling water for the fuel cell body.

【0014】さらに、分岐配管への手動弁を開放し、か
つ凝縮水の流量調整弁を通り水蒸気分離器へと至る配管
の手動弁を閉鎖して、凝縮水を全量を分岐配管から補給
水タンクおよび水処理装置を通して水蒸気分離器へ供給
する方法をとれば、仮に熱回収設備が清浄化されていな
くても燃料電池本体へは清浄な冷却水が供給されるの
で、従来不可能であった燃料電池本体と熱回収設備との
同時試運転の実施が可能となる。
Further, the manual valve to the branch pipe is opened, and the manual valve of the pipe leading to the steam separator through the flow control valve of the condensed water is closed, so that the entire amount of the condensed water is supplied from the branch pipe to the makeup water tank. And the method of supplying the water to the steam separator through the water treatment apparatus, the clean cooling water is supplied to the fuel cell body even if the heat recovery equipment is not cleaned, so that the fuel which was conventionally impossible Simultaneous test operation of the battery body and the heat recovery equipment can be performed.

【0015】[0015]

【実施例】図1は、本発明による燃料電池発電装置の蒸
気凝縮水循環装置の一実施例を示す基本系統図である。
図2に示した従来例と同一の機能を有する構成部品には
同一の符号が付されている。本図に示した蒸気凝縮水循
環装置の従来例との相違点は次のとおりである。
FIG. 1 is a basic system diagram showing one embodiment of a steam condensed water circulation device of a fuel cell power generator according to the present invention.
Components having the same functions as those of the conventional example shown in FIG. 2 are denoted by the same reference numerals. The difference between the steam condensed water circulating apparatus shown in the drawing and the conventional example is as follows.

【0016】水蒸気分離器5から外部の熱回収設備3
1へ蒸気を供給する配管に蒸気流量計11が付設されて
いる。 凝縮水タンク32から水蒸気分離器5へと凝縮水を戻
す配管に、凝縮水流量計12、この凝縮水流量計12と
上記の蒸気流量計11との検知信号により制御される流
量調整弁13、および手動弁15が付設されている。
An external heat recovery facility 3 from the steam separator 5
A steam flow meter 11 is attached to a pipe for supplying steam to the steam turbine 1. A pipe for returning condensed water from the condensed water tank 32 to the steam separator 5, a condensed water flow meter 12, a flow regulating valve 13 controlled by a detection signal from the condensed water flow meter 12 and the steam flow meter 11, And a manual valve 15.

【0017】また、凝縮水タンク32からの戻り配管
に、手動弁16を備えた凝縮水分岐配管17が設置され
補給水タンク21と連結されている。このように構成し
た蒸気凝縮水の循環装置においては、凝縮水の流量を流
量調整弁13により調整できるので、使用条件に適合し
た蒸気凝縮水の制御が可能となる。すなわち、 (1) 燃料電池発電装置の定常運転状態においては、蒸気
流量計11と凝縮水流量計12との検知信号により得ら
れる二つの流量が同一となるように流量調整弁13で凝
縮水流量を制御するものとすれば、水蒸気分離器5へ凝
縮水が定常的に供給されるので、水蒸気分離器5の温度
変動は微小に抑えられ、ほぼ一定した蒸気流量が熱回収
設備31へと送られる。したがって熱回収設備31を安
定して運転することができる。
A return pipe from the condensed water tank 32 is provided with a condensed water branch pipe 17 having a manual valve 16 and connected to the makeup water tank 21. In the steam condensed water circulation device configured as described above, the flow rate of the condensed water can be adjusted by the flow control valve 13, so that the steam condensed water can be controlled in accordance with the use conditions. (1) In the steady operation state of the fuel cell power generator, the flow rate regulating valve 13 controls the flow rate of the condensed water so that the two flow rates obtained by the detection signals of the steam flow meter 11 and the condensed water flow meter 12 become the same. Is controlled, the condensed water is supplied to the steam separator 5 constantly, so that the temperature fluctuation of the steam separator 5 is suppressed very small, and a substantially constant steam flow rate is sent to the heat recovery facility 31. Can be Therefore, the heat recovery facility 31 can be operated stably.

【0018】(2) また、長期の運転等により凝縮水の水
質が劣化し燃料電池本体の冷却水として不十分となった
場合には、凝縮水分岐配管17の手動弁16を開放し、
かつ蒸気流量計11と凝縮水流量計12との検知信号に
より、凝縮水流量が蒸気流量の一定割合R(0<R<
1)となるように凝縮水の流量調整弁13の弁開度を制
御するものとすれば、(1−R)の割合に対応する凝縮
水は分岐配管を通って補給水タンクに至り水処理装置を
通って清浄化された後水蒸気分離器へ供給されることと
なり、冷却水は全体として清浄化が進み水質が向上す
る。
(2) If the quality of the condensed water deteriorates due to long-term operation or the like and becomes insufficient as cooling water for the fuel cell body, the manual valve 16 of the condensed water branch pipe 17 is opened,
In addition, based on the detection signals from the steam flow meter 11 and the condensed water flow meter 12, the condensed water flow rate is set to a fixed rate R (0 <R <
If the valve opening of the flow rate control valve 13 for condensed water is controlled so as to satisfy 1), the condensed water corresponding to the ratio of (1-R) passes through the branch pipe to the makeup water tank, and is subjected to water treatment. After being purified through the apparatus, it is supplied to the steam separator, and the cooling water is entirely purified and the water quality is improved.

【0019】(3) さらに、凝縮水分岐配管17の手動弁
16を開放し、かつ手動弁15を閉鎖して、凝縮水の全
量を補給水タンク21および水処理装置23を通して水
蒸気分離器5へ供給する方法をとれば、仮に熱回収設備
31が清浄化されていなくても燃料電池本体1へは清浄
な冷却水が供給されるので、従来不可能であった燃料電
池本体1と熱回収設備31との同時試運転が可能とな
る。
(3) Further, the manual valve 16 of the condensed water branch pipe 17 is opened and the manual valve 15 is closed, and the entire amount of the condensed water is supplied to the steam separator 5 through the makeup water tank 21 and the water treatment device 23. If the supply method is adopted, clean cooling water is supplied to the fuel cell main body 1 even if the heat recovery equipment 31 is not cleaned. Simultaneous test operation with the X.31 is possible.

【0020】[0020]

【発明の効果】本発明においては、上述のように、燃料
電池本体へ冷却水を供給し、かつ冷却後の蒸気を導入す
る水蒸気分離器と、水蒸気分離器の蒸気を導入して熱を
取り出す熱回収設備と、熱回収設備で凝縮した水を貯え
る凝縮水タンクと、凝縮水タンクの凝縮水を前記水蒸気
分離器に再び戻す凝縮水ポンプとを有する燃料電池発電
装置の蒸気凝縮水循環装置において、水蒸気分離器から
熱回収設備へ供給される蒸気の流量測定手段と、凝縮水
タンクから水蒸気分離器へ送られる凝縮水の流量測定手
段と、凝縮水タンクから水蒸気分離器への配管系に組み
込まれ、上記の二つの流量測定手段により検知された流
量信号により制御される凝縮水の流量調整弁とを具備す
ることとし、さらにまた、凝縮水タンクから前記の凝縮
水の流量調整弁に至る配管に手動弁の開閉により補給水
タンクへと連通可能な分岐配管を設け、補給水を清浄化
する水処理装置を介して水蒸気分離器へと連結すること
としたので、 (1) 流量調整弁によって蒸気流量と流量調整弁を流れる
凝縮水流量とが同一となるように制御することにより、
水蒸気分離器へ凝縮水が定常的に供給されるので、水蒸
気分離器で発生する蒸気量の安定化が図られ、熱回収設
備の安定した運転が可能となった。
According to the present invention, as described above, a steam separator for supplying cooling water to the fuel cell main body and introducing steam after cooling, and introducing steam from the steam separator to extract heat. Heat recovery equipment, a condensed water tank for storing water condensed in the heat recovery equipment, and a condensed water pump for returning the condensed water in the condensed water tank to the steam separator again in a steam condensed water circulation device for a fuel cell power generator, The flow rate measuring means of the steam supplied from the steam separator to the heat recovery equipment, the flow rate measuring means of the condensed water sent from the condensed water tank to the steam separator, and the piping system from the condensed water tank to the steam separator are incorporated. A condensed water flow control valve controlled by a flow signal detected by the above two flow measuring means, and further from the condensed water tank to the condensed water flow control valve. A branch pipe that can communicate with the make-up water tank by opening and closing a manual valve is provided in the pipe to be connected to the steam separator through a water treatment device that purifies the make-up water. By controlling the steam flow rate and the condensed water flow rate flowing through the flow rate adjustment valve by the valve,
Since the condensed water is constantly supplied to the steam separator, the amount of steam generated in the steam separator was stabilized, and the stable operation of the heat recovery equipment became possible.

【0021】(2) また、流量調整弁を流れる凝縮水流量
と蒸気流量との割合を一定に保持し、凝縮水の一部を分
岐配管を通し水処理装置を介して水蒸気分離器へと戻す
よう制御することにより、凝縮水の清浄化を可能とし、
水質のレベルを一定範囲に保持することが可能となっ
た。 (3) さらにまた、凝縮水の全量を分岐配管を通し水処理
装置を介して水蒸気分離器へと戻すよう制御することに
より、熱回収設備の試運転を燃料電池発電装置の試運転
と同時に行うことができ、試験期間の短縮が可能となっ
た。
(2) The ratio between the flow rate of the condensed water and the flow rate of the steam flowing through the flow control valve is kept constant, and a part of the condensed water is returned to the steam separator through the branch pipe and the water treatment device. By controlling the condensate water,
It has become possible to maintain the water quality level within a certain range. (3) Further, by controlling the entire amount of condensed water to return to the steam separator through the branch pipe through the water treatment device, the test operation of the heat recovery equipment can be performed simultaneously with the test operation of the fuel cell power generator. The test period can be shortened.

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

【図1】本発明による燃料電池発電装置の蒸気凝縮水循
環装置の一実施例を示す基本系統図
FIG. 1 is a basic system diagram showing one embodiment of a steam condensed water circulation device of a fuel cell power generation device according to the present invention.

【図2】従来の燃料電池発電装置の蒸気凝縮水循環装置
を示す基本系統図
FIG. 2 is a basic system diagram showing a steam condensed water circulation device of a conventional fuel cell power generator.

【符号の説明】[Explanation of symbols]

1 燃料電池本体 4 冷却板 5 水蒸気分離器 9 循環ポンプ 10 圧力調整弁 11 蒸気流量計 12 凝縮水流量計 13 流量調整弁 14 制御弁 15、16 手動弁 17 分岐配管 21 補給水タンク 22 補給水供給ポンプ 23 水処理装置 24 補給水制御弁 31 熱回収設備 32 凝縮水タンク 33 凝縮水ポンプ DESCRIPTION OF SYMBOLS 1 Fuel cell main body 4 Cooling plate 5 Steam separator 9 Circulation pump 10 Pressure regulating valve 11 Steam flow meter 12 Condensed water flow meter 13 Flow regulating valve 14 Control valve 15, 16 Manual valve 17 Branch pipe 21 Makeup water tank 22 Supply water Pump 23 water treatment device 24 makeup water control valve 31 heat recovery equipment 32 condensed water tank 33 condensed water pump

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭59−73855(JP,A) 特開 昭60−208067(JP,A) 特開 平2−168573(JP,A) 特開 平2−10664(JP,A) 特開 平5−41232(JP,A) 特開 平5−211066(JP,A) 特開 平6−275294(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 8/04 H01M 8/06 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-59-73855 (JP, A) JP-A-60-208067 (JP, A) JP-A-2-168573 (JP, A) JP-A-2- 10664 (JP, A) JP-A-5-41232 (JP, A) JP-A-5-211066 (JP, A) JP-A-6-275294 (JP, A) (58) Fields investigated (Int. 7 , DB name) H01M 8/04 H01M 8/06

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】燃料電池本体へ冷却水を供給しかつ冷却後
の蒸気を導入する水蒸気分離器と、前記水蒸気分離器よ
り蒸気を導入して熱を取り出す熱回収設備と、前記熱回
収設備で凝縮した水を貯える凝縮水タンクと、前記凝縮
水タンクの凝縮水を前記水蒸気分離器に供給する凝縮水
ポンプとを有するものにあって、前記水蒸気分離器から
前記熱回収設備へ送られる蒸気の流量測定手段と、前記
凝縮水タンクから前記水蒸気分離器へ送られる凝縮水の
流量測定手段と、前記凝縮水タンクから前記水蒸気分離
器への配管系に組み込まれ、前記の二つの流量測定手段
により検知される流量信号により制御される流量調整弁
とを具備したことを特徴とする燃料電池発電装置の蒸気
凝縮水循環装置。
1. A steam separator for supplying cooling water to a fuel cell main body and introducing steam after cooling, a heat recovery facility for introducing steam from the steam separator and extracting heat, and a heat recovery facility. A condensed water tank for storing condensed water, and a condensed water pump for supplying condensed water in the condensed water tank to the steam separator, wherein the steam sent from the steam separator to the heat recovery facility is The flow rate measuring means, the flow rate measuring means of the condensed water sent from the condensed water tank to the steam separator, and incorporated in the piping system from the condensed water tank to the steam separator, the two flow rate measuring means A steam condensed water circulation device for a fuel cell power generator, comprising: a flow control valve controlled by a detected flow signal.
【請求項2】請求項1記載の燃料電池発電装置の蒸気凝
縮水循環装置において、前記凝縮水タンクから前記流量
調整弁へ至る配管に、少なくとも開閉弁と水処理装置を
介して前記水蒸気分離器へと連結される分岐配管を設け
たことを特徴とする燃料電池発電装置の蒸気凝縮水循環
装置。
2. A steam condensate circulating apparatus for a fuel cell power generator according to claim 1, wherein a pipe from said condensed water tank to said flow regulating valve is connected to said steam separator via at least an on-off valve and a water treatment device. A steam condensate circulating device for a fuel cell power generator, comprising a branch pipe connected to the steam generator.
【請求項3】請求項1記載の燃料電池発電装置の蒸気凝
縮水循環装置において、前記の蒸気の流量測定手段と前
記の凝縮水の流量測定手段とにより検知される二つの流
量が同一となるように前記流量調整弁を制御することを
特徴とする蒸気凝縮水循環装置の制御方法。
3. The steam condensed water circulation device for a fuel cell power generator according to claim 1, wherein the two flow rates detected by the steam flow rate measuring means and the condensed water flow rate measuring means are the same. And controlling the flow rate regulating valve.
【請求項4】請求項2記載の燃料電池発電装置の蒸気凝
縮水循環装置において、前記分岐配管に付設の開閉弁を
閉状態とし、前記の蒸気の流量測定手段と前記の凝縮水
の流量測定手段とにより検知される二つの流量が同一と
なるように前記流量調整弁を制御することを特徴とする
蒸気凝縮水循環装置の制御方法。
4. The steam condensed water circulation device for a fuel cell power generator according to claim 2, wherein an on-off valve attached to said branch pipe is closed, and said steam flow rate measuring means and said condensed water flow rate measuring means are provided. And controlling the flow rate regulating valve so that the two flow rates detected by the method are the same.
【請求項5】請求項2記載の燃料電池発電装置の蒸気凝
縮水循環装置において、前記分岐配管に付設の開閉弁を
開状態とし、前記の凝縮水の流量測定手段により検知さ
れる流量と前記の蒸気の流量測定手段により検知される
流量との比が一定となるように前記流量調整弁を制御す
ることを特徴とする蒸気凝縮水循環装置の制御方法。
5. The steam condensate water circulating device for a fuel cell power generator according to claim 2, wherein an on-off valve attached to said branch pipe is opened, and said flow rate detected by said flow rate measuring means of said condensed water and said flow rate A method for controlling a steam condensed water circulation device, wherein the flow rate control valve is controlled so that a ratio with a flow rate detected by a steam flow rate measuring means is constant.
【請求項6】請求項2記載の燃料電池発電装置の蒸気凝
縮水循環装置において、前記凝縮水タンクからの凝縮水
の全量を前記分岐配管に流通し、前記水処理装置を介し
て前記水蒸気分離器へと循環することを特徴とする蒸気
凝縮水循環装置の制御方法。
6. The steam condensate circulating device for a fuel cell power generator according to claim 2, wherein the entire amount of condensed water from said condensed water tank flows through said branch pipe, and said steam separator is passed through said water treatment device. A method for controlling a steam condensed water circulating apparatus, characterized by circulating water.
JP18795694A 1994-08-10 1994-08-10 Steam condensed water circulation device for fuel cell power generator and control method thereof Expired - Fee Related JP3280164B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18795694A JP3280164B2 (en) 1994-08-10 1994-08-10 Steam condensed water circulation device for fuel cell power generator and control method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18795694A JP3280164B2 (en) 1994-08-10 1994-08-10 Steam condensed water circulation device for fuel cell power generator and control method thereof

Publications (2)

Publication Number Publication Date
JPH0850907A JPH0850907A (en) 1996-02-20
JP3280164B2 true JP3280164B2 (en) 2002-04-30

Family

ID=16215113

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3280164B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100494944B1 (en) * 2003-07-28 2005-06-13 현대자동차주식회사 Cooling water system for fuel cell electric vehicle
JP5178041B2 (en) * 2007-04-25 2013-04-10 京セラ株式会社 Fuel cell device
JP5178042B2 (en) * 2007-04-25 2013-04-10 京セラ株式会社 Fuel cell device

Also Published As

Publication number Publication date
JPH0850907A (en) 1996-02-20

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