[go: up one dir, main page]

JP2001065975A - Cogeneration system - Google Patents

Cogeneration system

Info

Publication number
JP2001065975A
JP2001065975A JP24048899A JP24048899A JP2001065975A JP 2001065975 A JP2001065975 A JP 2001065975A JP 24048899 A JP24048899 A JP 24048899A JP 24048899 A JP24048899 A JP 24048899A JP 2001065975 A JP2001065975 A JP 2001065975A
Authority
JP
Japan
Prior art keywords
hot water
temperature
water
mixing
tank
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
JP24048899A
Other languages
Japanese (ja)
Inventor
Mikio Sei
三喜男 清
Mikio Shinagawa
幹夫 品川
Yuichiro Yasuda
雄一郎 安田
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP24048899A priority Critical patent/JP2001065975A/en
Publication of JP2001065975A publication Critical patent/JP2001065975A/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
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/14Combined heat and power generation [CHP]

Landscapes

  • Heat-Pump Type And Storage Water Heaters (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a cogeneration system which can supply hot water at a set temperature in a stable manner. SOLUTION: A heat exchanger 2 is provided for a hot water storage tank 1 to effect recovery of waste heat by effecting heat exchange with water in the tank 1, while hot water stored in the tank 1 is supplied through a temperature raising means 3 whose heating capacity is variable. A mixing means 4, wherein cooled water is fed and mixed into the hot water sent from the tank 1 to the temperature raising means 3, is provided. When the hot water of the tank 1 has a temperature higher than a set temperature, by mixing the cooled water to lower the temperature of the hot water so that water of the set temperature can be supplied. If the temperature of the hot water of the tank 1 is slightly lower than the set temperature, the mixing ratio of cooled water is raised to lower the temperature of the hot water, which water is fed to the temperature raising means 3 to heat it using a heating capacity of lower limit of the means 3, whereby the hot water can be heated to the set temperature and supplied.

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】本発明は、燃料電池やガスエ
ンジンなどの発電機を用いて発電を行なうと共に温水を
得て給湯するようにしたコージェネレーションシステム
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cogeneration system which generates electric power by using a generator such as a fuel cell or a gas engine, and obtains hot water and supplies hot water.

【0002】[0002]

【従来の技術】燃料電池やガスエンジンなどを用いて発
電を行なうと共に、その発電の際に発生する排熱を利用
して水を加熱し、給湯を行なうようにしたコージェネレ
ーションシステムが実用化されている。コージェネレー
ションシステムとして、温水を蓄える貯湯槽を備え、貯
湯槽内の水と発電の際に発生する排熱とを熱交換するた
めの熱交換器を設けて形成されたものがある。そしてこ
のような給湯を行なうコージェネレーションシステムに
おいて、貯湯槽に給水される水道水等の水温は季節によ
って変動するので、貯湯槽内の温水の水温も季節によっ
て変動し、また給湯量や排熱の発生量によっても貯湯槽
内の温水の水温は変動する。このために、ユーザーが設
定した一定の湯温で給湯することが難しい。
2. Description of the Related Art A cogeneration system has been put into practical use in which a fuel cell or a gas engine is used to generate electric power, and water is heated by using waste heat generated during the electric power generation to supply hot water. ing. As a cogeneration system, there is a cogeneration system provided with a hot water tank for storing hot water, and provided with a heat exchanger for exchanging heat between water in the hot water tank and waste heat generated during power generation. In such a cogeneration system that supplies hot water, since the temperature of tap water or the like supplied to the hot water tank varies with the season, the temperature of the hot water in the hot water tank also varies with the season, and the amount of hot water and the amount of exhaust heat The temperature of the hot water in the hot water tank also fluctuates depending on the generation amount. For this reason, it is difficult to supply hot water at a constant hot water temperature set by the user.

【0003】そこで、特開平8-28955号公報など
では、貯湯槽の温水を所定の一定温度に加熱して供給す
るようにしている。図2はその一例を示すものであり、
1は貯湯槽、2は熱交換器、15は発電機、16はクー
リングタワー、17は発電機15と熱交換器2の間の排
熱回収ラインである。貯湯槽1には給水ライン18から
給水されるようにしてあり、熱交換器2に給水された水
は、発電機15からの排熱と熱交換器2で熱交換され、
加熱される。また貯湯槽1には給湯ライン19が接続し
てあり、給湯ライン19の先部には給湯栓20が設けて
ある。この給湯ライン19の途中にはボイラーやヒート
ポンプなどで形成される昇温手段3が設けてあり、さら
に貯湯槽1と給湯栓20を短絡して接続するバイパスラ
イン21が接続してある。そして熱交換器2で加熱され
て貯湯槽1内に蓄えられた温水は、給湯ライン19を通
して給湯栓20に給湯されるが、水温検出センサー22
で検出される水温が所定の設定温度と同一かこれよりも
高いと、三方弁23の切り換えで貯湯槽1内の温水はバ
イパスライン21を通って給湯栓20へと給湯される。
また、水温検出センサー22で検出される水温が所定の
設定温度より低い場合は、三方弁23の切り換えで貯湯
槽1内の温水は昇温手段3に供給され、昇温手段3で所
定温度にまで加熱された後に、給湯栓20へと給湯され
る。このようにして、所定の設定された温度より低い温
水が給湯されることをなくして、使い勝手を向上させて
いるのである。
Therefore, in Japanese Patent Application Laid-Open No. 8-28955, hot water in a hot water storage tank is heated to a predetermined constant temperature and supplied. FIG. 2 shows an example thereof.
1 is a hot water storage tank, 2 is a heat exchanger, 15 is a generator, 16 is a cooling tower, and 17 is an exhaust heat recovery line between the generator 15 and the heat exchanger 2. The hot water storage tank 1 is supplied with water from a water supply line 18, and the water supplied to the heat exchanger 2 exchanges heat with the waste heat from the generator 15 in the heat exchanger 2,
Heated. A hot water supply line 19 is connected to the hot water storage tank 1, and a hot water tap 20 is provided at a leading end of the hot water supply line 19. In the middle of the hot water supply line 19, a temperature raising means 3 formed by a boiler, a heat pump or the like is provided, and a bypass line 21 for short-circuiting and connecting the hot water storage tank 1 and the hot water tap 20 is connected. The hot water heated by the heat exchanger 2 and stored in the hot water storage tank 1 is supplied to a hot water tap 20 through a hot water supply line 19.
When the water temperature detected in step (1) is equal to or higher than the predetermined set temperature, the hot water in the hot water storage tank 1 is supplied to the hot water tap 20 through the bypass line 21 by switching the three-way valve 23.
When the water temperature detected by the water temperature detection sensor 22 is lower than a predetermined set temperature, the hot water in the hot water storage tank 1 is supplied to the temperature raising means 3 by switching the three-way valve 23, and the temperature is raised to the predetermined temperature by the temperature raising means 3. Then, the hot water is supplied to hot water tap 20. In this way, hot water having a temperature lower than the predetermined temperature is not supplied, and the usability is improved.

【0004】[0004]

【発明が解決しようとする課題】しかしながら図2のも
のでは、貯湯槽1に蓄えられる温水の温度が所定の設定
温度より低い場合は、昇温手段3で設定温度にまで加熱
して給湯することができるものの、貯湯槽1に蓄えられ
る温水の温度が所定の設定温度より高い場合には、湯温
を調整することができず、高い水温のまま給湯されてし
まうものであり、この点で使い勝手が良いとはいえな
い。
However, in FIG. 2, when the temperature of the hot water stored in the hot water storage tank 1 is lower than a predetermined set temperature, the hot water is heated to the set temperature by the temperature raising means 3 to supply hot water. However, if the temperature of the hot water stored in the hot water storage tank 1 is higher than a predetermined set temperature, the hot water temperature cannot be adjusted, and the hot water is supplied at a high water temperature. Is not good.

【0005】また、昇温手段3として通常利用されるボ
イラーやヒートポンプなど加熱能力が可変な加熱源は、
加熱の制御範囲に下限値が存在し、例えば大阪ガス
(株)製給湯器「RN−A524RFW」の場合、ガス
バーナーの制御に伴う制御下限値があるため、制御範囲
は2.5号〜24号の間である。従って、貯湯槽1の温
水の水温が設定温度より少しだけ低い場合、昇温手段3
を作動させて下限の能力で加熱しても、温水の水温は設
定温度を超えてしまうことがあり、この場合には、昇温
手段3で加熱して設定温度を超えた温水を給湯するか、
昇温手段3を作動させずに設定温度より低いままの温水
を給湯するかのいずれかになる。すなわち、この給湯器
を例にとると、下限の2.5号で加熱を行なうかもしく
は加熱を行なわないかのオンオフ制御になり、給湯の湯
温が安定しなくなるという問題を有するものであった。
A heating source having a variable heating capacity, such as a boiler or a heat pump, which is usually used as the temperature raising means 3, comprises:
There is a lower limit in the heating control range. For example, in the case of the hot water heater “RN-A524RFW” manufactured by Osaka Gas Co., Ltd., there is a control lower limit associated with the control of the gas burner. It is between issues. Therefore, when the temperature of the hot water in the hot water storage tank 1 is slightly lower than the set temperature,
, The temperature of the hot water may exceed the set temperature even if the heater is heated at the lower limit capacity. In this case, it is necessary to heat the hot water by the temperature raising means 3 and supply hot water exceeding the set temperature. ,
Either hot water with a temperature lower than the set temperature is supplied without operating the temperature raising means 3. That is, taking this water heater as an example, on / off control of whether to perform heating at the lower limit of No. 2.5 or no heating is performed, and there is a problem that the temperature of the hot water becomes unstable. .

【0006】本発明は上記の点に鑑みてなされたもので
あり、設定温度の温水を安定して給湯することができる
コージェネレーションシステムを提供することを目的と
するものである。
The present invention has been made in view of the above points, and has as its object to provide a cogeneration system capable of stably supplying hot water at a set temperature.

【0007】[0007]

【課題を解決するための手段】本発明の請求項1に係る
コージェネレーションシステムは、貯湯槽1に貯湯槽1
内の水と熱交換して排熱を回収する熱交換器2を設ける
と共に、貯湯槽1内に蓄えられた温水を加熱能力可変の
昇温手段3を介して給湯するようにしたコージェネレー
ションシステムにおいて、貯湯槽1と昇温手段3との間
に、貯湯槽1から昇温手段3に送られる温水に冷水を給
水して混合可能なミキシング手段4を備えて成ることを
特徴とするものである。
According to a first aspect of the present invention, there is provided a cogeneration system comprising: a hot water tank;
Cogeneration system in which a heat exchanger 2 for exchanging heat with water in the tank and recovering waste heat is provided, and hot water stored in a hot water storage tank 1 is supplied through a heating means 3 having a variable heating capacity. , Characterized in that mixing means 4 is provided between the hot water tank 1 and the temperature raising means 3, which is capable of supplying cold water to hot water sent from the hot water tank 1 to the temperature raising means 3 and mixing the same. is there.

【0008】また請求項2の発明は、請求項1におい
て、ミキシング手段4と昇温手段3との間に、流水量及
び水温を計測する第一の計測手段5を備え、第一の計測
手段5で計測された流水量及び水温に基づいて、ミキシ
ング手段4で混合する温水と冷水の比率を制御して成る
ことを特徴とするものである。
According to a second aspect of the present invention, in the first aspect, a first measuring means 5 for measuring a flowing water amount and a water temperature is provided between the mixing means 4 and the temperature raising means 3, and the first measuring means is provided. The ratio of hot water to cold water mixed by the mixing means 4 is controlled based on the amount of flowing water and the water temperature measured in 5.

【0009】また請求項3の発明は、請求項1又は2に
おいて、貯湯槽1とミキシング手段4との間に、流水量
及び水温を計測する第二の計測手段6を備えると共に、
ミキシング手段4に給水する冷水の流水量及び水温を計
測する第三の計測手段7を備え、第二及び第三の計測手
段6,7で計測された流水量及び水温に基づいて、ミキ
シング手段4で混合する温水と冷水の比率を制御して成
ることを特徴とするものである。
According to a third aspect of the present invention, in the first or second aspect, a second measuring means 6 for measuring a flowing water amount and a water temperature is provided between the hot water tank 1 and the mixing means 4,
A third measuring means 7 for measuring a flowing water amount and a water temperature of the cold water supplied to the mixing means 4 is provided, and based on the flowing water amounts and the water temperatures measured by the second and third measuring means 6 and 7, the mixing means 4 is provided. And controlling the ratio of hot water and cold water to be mixed.

【0010】また請求項4の発明は、請求項3におい
て、貯湯槽1内に蓄えられた温水の温度を計測する第四
の計測手段8を備え、第四の計測手段8で計測された水
温に基づいて、給湯開始時にミキシング手段4で混合す
る温水と冷水の比率を制御して成ることを特徴とするも
のである。
According to a fourth aspect of the present invention, in the third aspect, there is provided a fourth measuring means for measuring the temperature of the hot water stored in the hot water storage tank, and the water temperature measured by the fourth measuring means is provided. , The ratio of hot water and cold water mixed by the mixing means 4 at the start of hot water supply is controlled.

【0011】[0011]

【発明の実施の形態】以下、本発明の実施の形態を説明
する。
Embodiments of the present invention will be described below.

【0012】図1は本発明の実施の形態の一例を示すも
のであり、図1の実施の形態は、発電機として燃料電池
10を用いて給湯を行なうコージェネレーションシステ
ムを示すものである。燃料電池10は原燃料から水素リ
ッチな改質ガスを生成する改質器26を付随している。
改質器26には原燃料導入路27から炭化水素系の気
体、液体、固体や、メタノール系等のアルコール燃料な
どの原燃料が供給されるようになっており、原燃料と水
蒸気から水蒸気改質反応によって水素リッチな改質ガス
を生成するように形成してある。炭化水素系の気体とし
てはメタンガス、プロパンガス、ブタンガス、液化石油
ガス等を、炭化水素系の液体としては灯油、軽油、ガソ
リン等を、アルコール燃料としてはメタノール、エタノ
ール等を例示することができる。家庭用の用途では、入
手のし易さ及び取り扱い性から、プロパンガス、ブタン
ガス、メタンガスを主成分としたガスや灯油が好まし
い。原燃料として天然ガス(主成分メタンガス)を用
い、改質器26で水蒸気改質反応によって水素リッチな
改質ガスを生成させる反応を次に示す。
FIG. 1 shows an example of an embodiment of the present invention, and the embodiment of FIG. 1 shows a cogeneration system for supplying hot water using a fuel cell 10 as a generator. The fuel cell 10 has a reformer 26 that generates a hydrogen-rich reformed gas from the raw fuel.
The reformer 26 is supplied with a raw fuel such as a hydrocarbon-based gas, liquid, or solid, or an alcohol fuel such as a methanol-based fuel through a raw fuel introduction passage 27, and converts the raw fuel and steam into steam. It is formed so as to generate a hydrogen-rich reformed gas by a hydrogen reaction. Examples of the hydrocarbon-based gas include methane gas, propane gas, butane gas, and liquefied petroleum gas. Examples of the hydrocarbon-based liquid include kerosene, light oil, and gasoline. Examples of the alcohol fuel include methanol and ethanol. For home use, a gas or kerosene containing propane gas, butane gas, or methane gas as a main component is preferable in terms of availability and handleability. A reaction in which a natural gas (mainly methane gas) is used as a raw fuel to generate a hydrogen-rich reformed gas by a steam reforming reaction in the reformer 26 will be described below.

【0013】CH+2HO→4H+CO 上記の水蒸気改質反応には高温での触媒反応が必要であ
り、このため、改質器26内を所定の温度(600〜7
00℃)に加熱するようにしてある。加熱方法は特に限
定されるものではないが、原燃料である天然ガスなどを
燃焼させて加熱を行なうことができる。この燃焼によっ
て発生する排気ガスは排気経路28から排出されるよう
にしてあり、また改質器26で生成された水素リッチな
改質ガスはガス供給管29から送り出されるようにして
ある。
CH 4 + 2H 2 O → 4H 2 + CO 2 The above-mentioned steam reforming reaction requires a catalytic reaction at a high temperature. Therefore, the inside of the reformer 26 is heated to a predetermined temperature (600 to 7).
(00 ° C.). The heating method is not particularly limited, but heating can be performed by burning natural gas or the like as a raw fuel. The exhaust gas generated by this combustion is exhausted from an exhaust path 28, and the hydrogen-rich reformed gas generated in the reformer 26 is sent out from a gas supply pipe 29.

【0014】上記のように改質器26で生成された改質
ガスはガス供給管29から燃料電池10を構成する複数
のセル30のアノード部に供給され、カソード部には酸
素を含む空気を供給することで、改質ガス中の水素と空
気中の酸素から発電が行なわれるようになっている。燃
料電池10としては、リン酸型や溶融炭酸塩型、固体高
分子型など各種のものがあるが、蒸気を利用しない給湯
と発電のみのコージェネレーションシステムにおいて
は、比較的低温で作動する固体高分子型が望ましい。こ
のように発電された電気は送電線31を通じて外部の各
種の電気機器に送電される。送電は電気機器に直接行な
うのではなく、インバータ等を組み合わせて行なうよう
にしてもよい。
The reformed gas generated by the reformer 26 as described above is supplied from the gas supply pipe 29 to the anodes of a plurality of cells 30 constituting the fuel cell 10, and the cathode contains air containing oxygen. By supplying, power is generated from hydrogen in the reformed gas and oxygen in the air. As the fuel cell 10, there are various types such as a phosphoric acid type, a molten carbonate type, and a solid polymer type. However, in a cogeneration system using only hot water supply and power generation without using steam, a solid high-temperature system operating at a relatively low temperature is used. Molecular form is preferred. The electricity generated in this way is transmitted to various external electric devices via the transmission line 31. The power transmission may not be performed directly to the electric equipment, but may be performed by combining an inverter and the like.

【0015】このように燃料電池10で発電を行なう際
に、改質器26や燃料電池10のセル30から排熱が発
生するので、この排熱を回収する熱交換手段が設けてあ
る。この熱交換手段としては各種あるが、例えば、燃料
電池10の各セル30に付設した熱交換器32や改質器
26の排気経路28に付設した熱交換器33を用いるよ
うにしてあり、これらの熱交換器32,33の間には熱
媒循環路34が接続してあり、熱媒循環用ポンプ35に
よって熱媒を循環させるようにしてある。
When power is generated in the fuel cell 10 as described above, waste heat is generated from the reformer 26 and the cells 30 of the fuel cell 10, and a heat exchange means for recovering the waste heat is provided. There are various heat exchange means. For example, a heat exchanger 32 attached to each cell 30 of the fuel cell 10 and a heat exchanger 33 attached to the exhaust path 28 of the reformer 26 are used. A heat medium circulating path 34 is connected between the heat exchangers 32 and 33, and a heat medium circulating pump 35 circulates the heat medium.

【0016】一方、貯湯槽1には上端部と下端部に接続
して温水循環路36が設けてあり、温水循環ポンプ37
によって貯湯槽1内の温水を循環させるようにしてあ
る。この温水循環路36の蛇行させた熱交換部36aと
上記熱媒循環路34の蛇行させた熱交換部34aをケー
シング内で近接配置することによって、熱交換器2を形
成するようにしてある。熱交換器2,32,33として
は、流体同士で熱交換を行なうものであれば、特に制限
されることなくどのようなものでも使用することができ
る。
On the other hand, the hot water tank 1 is provided with a hot water circulation path 36 connected to the upper end and the lower end thereof.
The hot water in the hot water storage tank 1 is circulated. The heat exchanger 2 is formed by disposing the meandering heat exchange part 36a of the hot water circulation path 36 and the meandering heat exchange part 34a of the heat medium circulation path 34 in the casing. The heat exchangers 2, 32, and 33 are not particularly limited as long as they perform heat exchange between fluids.

【0017】貯湯槽1にはさらに、その下端部に給水口
40を設けてこの給水口40に水道配管などの給水路4
1が接続してあり、水道水などの冷水が貯湯槽1内に給
水されるようにしてある。また貯湯槽1の上端部に給湯
口42を設けて給湯路43が接続してあり、この給湯路
43は昇温手段3に接続してある。昇温手段3は貯湯槽
1の温水の補助加熱源となるものであり、ガスや灯油を
用いたボイラー、電熱ヒータ、ヒートポンプなど加熱能
力が可変のもの、つまり温水の温度に応じて加熱熱量を
変化させ、所定の設定温度にまで昇温させるように温水
を加熱することができるもので形成してある。
The hot water storage tank 1 is further provided with a water supply port 40 at a lower end thereof, and the water supply port 40 is provided with a water supply passage 4 such as a water supply pipe.
1 is connected so that cold water such as tap water is supplied into the hot water storage tank 1. A hot water supply port 42 is provided at the upper end of the hot water storage tank 1, and a hot water supply path 43 is connected to the hot water supply path 43. The hot water supply path 43 is connected to the temperature raising means 3. The temperature raising means 3 serves as an auxiliary heating source of hot water in the hot water storage tank 1 and has a variable heating capacity such as a boiler using gas or kerosene, an electric heater, or a heat pump. It is formed of a material that can be heated to heat the hot water so as to change the temperature to a predetermined set temperature.

【0018】上記のように形成されるコージェネレーシ
ョンシステムにあって、熱媒循環ポンプ35を作動させ
て熱媒循環路34の熱媒を熱交換器32,33を通す
と、熱媒は燃料電池10のセル30や改質器26の排気
経路28の排熱と熱交換されて加熱される。一方、温水
循環ポンプ37を作動させて貯湯槽1内の温水(水)を
温水循環路36に循環させると、この温水は、上記のよ
うに排熱と熱交換されて加熱された熱媒循環路34の熱
媒と熱交換器2内で熱交換され、昇温される。このよう
にして貯湯槽1内の温水は、燃料電池10を発電させる
際の排熱を回収すると共に熱交換して昇温され、高温の
温水として貯湯槽1に貯えられるものである。そして貯
湯槽1に貯えられた温水は、給水口40から冷水を貯湯
槽1内に給水することによって、給湯口42から給湯路
43に押し出されて給湯されるものであり、温水の温度
が設定温度より低いときには昇温手段3で所定の設定温
度にまで加熱された後、蛇口等に給湯されるようになっ
ている。
In the cogeneration system formed as described above, when the heat medium circulating pump 35 is operated to pass the heat medium in the heat medium circulation path 34 through the heat exchangers 32 and 33, the heat medium is The heat is exchanged with the exhaust heat of the exhaust cell 28 of the cell 30 and the reformer 26 and heated. On the other hand, when the hot water circulation pump 37 is operated to circulate the hot water (water) in the hot water storage tank 1 through the hot water circulation path 36, the hot water is exchanged with the exhaust heat as described above, and the heated heat medium circulates. The heat is exchanged with the heat medium in the passage 34 in the heat exchanger 2 to increase the temperature. In this way, the hot water in the hot water storage tank 1 recovers waste heat when the fuel cell 10 generates electric power, exchanges heat and raises the temperature, and is stored in the hot water storage tank 1 as high-temperature hot water. The hot water stored in the hot water storage tank 1 is supplied by supplying cold water from the water supply port 40 into the hot water storage tank 1 to be pushed out of the hot water supply port 42 into the hot water supply path 43 and supplied with hot water. When the temperature is lower than the predetermined temperature, the temperature is raised to a predetermined set temperature by the temperature raising means 3 and then supplied to a faucet or the like.

【0019】ここで、貯湯槽1と昇温手段3の間の給湯
路43には水道配管などの給水路44が接続してあり、
貯湯槽1から給湯路43に供給される温水に給水路44
から水道水などの冷水を供給して、温水と冷水とをミキ
シングすることができるようにしてある。ミキシング手
段4は給湯路43と給水路44にそれぞれ流水量を制御
可能なバルブを設けて形成するようにしてもよいが、給
湯量を蛇口等で自由に設定できるためには、給湯路43
と給水路44の接続部にミキシングバルブを設けてミキ
シング手段4を形成するのが好ましい。
Here, a hot water supply path 44 such as a water supply pipe is connected to a hot water supply path 43 between the hot water storage tank 1 and the temperature raising means 3.
The hot water supplied from the hot water storage tank 1 to the hot water supply channel 43 is supplied to the hot water supply channel 44.
And cold water such as tap water supplied from the company to mix hot and cold water. The mixing means 4 may be formed by providing a valve capable of controlling the amount of flowing water in each of the hot water supply path 43 and the water supply path 44. However, in order to be able to freely set the hot water supply amount with a faucet or the like, the mixing means 4 is required.
It is preferable to form a mixing means 4 by providing a mixing valve at the connection between the water supply path 44 and the water supply passage 44.

【0020】そして、ミキシング手段4による温水と冷
水の混合比率の制御は、ミキシング手段4と昇温手段3
の間において給湯路43に設けた水温センサー5a及び
流量センサー5bからなる第一計測手段5によって行な
うことができる。すなわち、ミキシング手段4で冷水と
ミキシングされた後の温水の温度を水温センサー5aで
計測すると共にこの温水の流量を流量センサー5bで計
測し、例えば温水の計測温度が設定温度より高いときに
は、その温度と流量に応じて給水路44からの冷水の供
給量を増加させたり給湯口42からの温水の供給量を減
少させたりして、冷水の混合比率を高めるようにし、ま
た温水の計測温度が設定温度より低いときには、その温
度と流量に応じて給水路44からの冷水の供給量を減少
させたり給湯口42からの温水の供給量を増加させたり
して、温水の混合比率を高めるようにするものである。
The mixing means 4 controls the mixing ratio of hot water and cold water by mixing the mixing means 4 with the heating means 3.
This can be performed by the first measuring means 5 including the water temperature sensor 5a and the flow rate sensor 5b provided in the hot water supply passage 43. That is, the temperature of the hot water mixed with the cold water by the mixing means 4 is measured by the water temperature sensor 5a and the flow rate of the hot water is measured by the flow rate sensor 5b. For example, when the measured temperature of the hot water is higher than the set temperature, the temperature is measured. By increasing the supply amount of cold water from the water supply passage 44 or decreasing the supply amount of hot water from the hot water supply port 42 according to the flow rate, the mixing ratio of the cold water is increased, and the measured temperature of the hot water is set. When the temperature is lower than the temperature, the mixing ratio of the hot water is increased by decreasing the supply amount of the cold water from the water supply passage 44 or increasing the supply amount of the hot water from the hot water supply port 42 according to the temperature and the flow rate. Things.

【0021】ミキシング手段4による温水と冷水の混合
比率の制御は、この他に、貯湯槽1とミキシング手段4
の間において給湯路43に設けた水温センサー6a及び
流量センサー6bからなる第二計測手段6と、給水路4
4に設けた水温センサー7a及び流量センサー7bから
なる第三計測手段7とによって行なうことができる。す
なわち、貯湯槽1から供給される温水の温度を水温セン
サー6aで計測すると共にこの温水の流量を流量センサ
ー6bで計測し、また給水路44から給水される冷水の
温度を水温センサー7aで計測すると共にこの温水の流
量を流量センサー7bで計測し、温水の温度と流量及び
冷水の温度と流量からミキシング手段4でミキシングさ
れた後の温水の温度を演算することで、温水と冷水の混
合比率を求めて制御することができるものである。この
場合、上記の流量センサー5bを併用するときには、流
量センサー6b,7bの一方は省略可能である。これ
は、流量センサー5bの計測値から流量センサー7bの
計測値を差し引くことで、流量センサー6bがなくとも
貯湯槽1からの温水の流量を求めることができ、また流
量センサー5bの計測値から流量センサー6bの計測値
を差し引くことで、流量センサー7bがなくとも給水路
44からの冷水の流量を求めることができるからであ
る。逆にいえば、流量センサー6b,7bがあれば流量
センサー5bがなくとも、昇温手段3に供給される流量
を求めることができる。
The mixing ratio of the hot water and the cold water by the mixing means 4 is controlled in addition to the hot water tank 1 and the mixing means 4.
A second measuring means 6 including a water temperature sensor 6a and a flow rate sensor 6b provided in the hot water supply passage 43;
4 can be performed by the third measuring means 7 including the water temperature sensor 7a and the flow rate sensor 7b. That is, the temperature of the hot water supplied from the hot water storage tank 1 is measured by the water temperature sensor 6a, the flow rate of the hot water is measured by the flow rate sensor 6b, and the temperature of the cold water supplied from the water supply passage 44 is measured by the water temperature sensor 7a. At the same time, the flow rate of the hot water is measured by the flow rate sensor 7b, and the temperature of the hot water mixed by the mixing means 4 is calculated from the temperature and the flow rate of the hot water and the temperature and the flow rate of the cold water, so that the mixing ratio of the hot water and the cold water is calculated. It can be sought and controlled. In this case, when the flow sensor 5b is used together, one of the flow sensors 6b and 7b can be omitted. This is because the flow rate of the hot water from the hot water storage tank 1 can be obtained without the flow rate sensor 6b by subtracting the measurement value of the flow rate sensor 7b from the measurement value of the flow rate sensor 5b. This is because the flow rate of the chilled water from the water supply passage 44 can be obtained without the flow rate sensor 7b by subtracting the measurement value of the sensor 6b. Conversely, if the flow sensors 6b and 7b are provided, the flow rate supplied to the temperature raising means 3 can be obtained without the flow sensor 5b.

【0022】また、貯湯槽1内の給湯口42近傍には温
度センサー8aからなる第四計測手段8設けてあり、給
湯口42近傍の温水の温度を測定するようにしてある。
そして、給湯の開始時には、この温度センサー8aで計
測された温水の温度に基づいてミキシング手段4でミキ
シングする温水と冷水の混合比率を制御し、給湯を開始
した後は、貯湯槽1とミキシング手段4の間において給
湯路43に設けた上記の水温センサー6aで計測された
温水の温度に基づいてミキシング手段4でミキシングす
る温水と冷水の混合比率を制御するようにすることによ
って、給湯開始時の温水と冷水の混合比率の制御を正確
に行なうことができるものである。すなわち、給湯開始
の際には給湯路43内の温水の温度は貯湯槽1に貯えら
れている温水よりも低く、給湯開始時にこの給湯路43
内の温水の温度に基づいて温水と冷水の混合比率を制御
すると、正確な混合比率で制御を行なうことができない
が、このように給湯開始時には貯湯槽1内の温水の温度
に基づいて温水と冷水の混合比率を制御すると、正確な
混合比率で制御を行なうことができるのである。
A fourth measuring means 8 comprising a temperature sensor 8a is provided near the hot water supply port 42 in the hot water storage tank 1 so as to measure the temperature of the hot water near the hot water supply port 42.
At the start of hot water supply, the mixing ratio of the hot water and the cold water to be mixed by the mixing means 4 is controlled based on the temperature of the hot water measured by the temperature sensor 8a, and after the hot water supply is started, the hot water storage tank 1 and the mixing means The mixing ratio between the hot water and the cold water to be mixed by the mixing means 4 is controlled based on the temperature of the hot water measured by the water temperature sensor 6a provided in the hot water supply passage 43 between the hot water supply channels 43 at the start of hot water supply. It is possible to accurately control the mixing ratio of hot water and cold water. That is, at the time of starting hot water supply, the temperature of the hot water in hot water supply path 43 is lower than the temperature of the hot water stored in hot water storage tank 1.
If the mixing ratio of hot water and cold water is controlled based on the temperature of hot water in the hot water supply, control cannot be performed with an accurate mixing ratio. By controlling the mixing ratio of the cold water, the control can be performed with an accurate mixing ratio.

【0023】上記のように各計測手段5〜8による計測
結果に基づいてミキシング手段4でミキシングする温水
と冷水の混合比率を制御するにあたって、冷水が混合さ
れた温水の温度がユーザーによって設定された温度に近
くなるように、混合比率の制御を行なうものである。た
だし、既述のように、加熱能力が可変な昇温手段3は加
熱の制御範囲に下限値が存在し、例えば大阪ガス(株)
製給湯器「RN−A524RFW」の場合、制御範囲は
2.5号〜24号の間であり、貯湯槽1の温水が設定温
度より少し低い場合、下限の能力の2.5号で加熱を行
なっても加熱後の温水の水温は設定温度を超えてしまう
ことがある。そこでこの場合には、給水路44から給湯
路43に給水する冷水の量を増加させて冷水の混合比率
を高めるように制御するものであり、昇温手段3に供給
される温水の温度を下げ、昇温手段3の下限の加熱能力
でこの温水を加熱することによって、加熱された温水の
水温が設定温度になるようにしてある。例えば、給湯す
る温水の設定温度が42℃の場合、昇温手段3に供給さ
れる温水の温度が40℃、流水量が5リットル/min
であると、昇温手段3において必要な加熱量は0.7k
Wである。これに対して、昇温手段3の下限の加熱能力
が2.5号であると、加熱量は4.4kWであるので、
昇温手段3で加熱された温水の温度は42℃を超えてし
まう。そこでこの場合には、ミキシング手段4で混合す
る冷水の比率を増加させて、昇温手段3に供給される温
水の温度が29.5℃になるように制御すると、昇温手
段3の下限の能力で加熱した温水の温度を設定された4
2℃にすることができる。このよにして、設定温度で安
定して給湯を行なうことが可能になるものである。
As described above, in controlling the mixing ratio of the hot water and the cold water to be mixed by the mixing means 4 based on the measurement results by the measuring means 5 to 8, the temperature of the hot water mixed with the cold water is set by the user. The mixing ratio is controlled so as to approach the temperature. However, as described above, the heating means 3 having a variable heating capacity has a lower limit in the heating control range. For example, Osaka Gas Co., Ltd.
In the case of the hot water heater "RN-A524RFW", the control range is between 2.5 and 24, and when the hot water in the hot water storage tank 1 is slightly lower than the set temperature, heating is performed at the lower limit capacity of 2.5. Even if it is performed, the temperature of the heated hot water may exceed the set temperature. Therefore, in this case, the amount of cold water supplied from the water supply passage 44 to the hot water supply passage 43 is controlled to increase the mixing ratio of the cold water, and the temperature of the hot water supplied to the temperature raising means 3 is reduced. By heating this hot water with the lower limit heating capacity of the temperature raising means 3, the temperature of the heated hot water becomes the set temperature. For example, when the set temperature of the hot water to be supplied is 42 ° C., the temperature of the hot water supplied to the temperature raising means 3 is 40 ° C., and the amount of flowing water is 5 liter / min.
, The heating amount required in the temperature raising means 3 is 0.7 k
W. On the other hand, if the lower limit heating capacity of the temperature raising means 3 is No. 2.5, the heating amount is 4.4 kW.
The temperature of the hot water heated by the temperature raising means 3 exceeds 42 ° C. Therefore, in this case, if the ratio of the cold water mixed by the mixing means 4 is increased to control the temperature of the hot water supplied to the temperature increasing means 3 to 29.5 ° C., the lower limit of the temperature increasing means 3 4 set the temperature of the hot water heated by the ability
It can be 2 ° C. In this manner, hot water can be supplied stably at the set temperature.

【0024】尚、昇温手段3に供給される温水が、昇温
手段3の加熱の制御範囲で加熱しても設定温度を越えな
い程度に低い場合には、上記と同様の制御は行なわず
に、昇温手段3による加熱をするようにしてもよい。
If the temperature of the hot water supplied to the temperature raising means 3 is low enough not to exceed the set temperature even if it is heated within the heating control range of the temperature raising means 3, the same control as described above is not performed. Alternatively, heating by the temperature raising means 3 may be performed.

【0025】[0025]

【発明の効果】上記のように請求項1の発明は、貯湯槽
に貯湯槽内の水と熱交換して排熱を回収する熱交換器を
設けると共に、貯湯槽内に蓄えられた温水を加熱能力可
変の昇温手段を介して給湯するようにしたコージェネレ
ーションシステムにおいて、貯湯槽と昇温手段との間
に、貯湯槽から昇温手段に送られる温水に冷水を給水し
て混合可能なミキシング手段を備えるので、貯湯槽の温
水が設定温度より高い場合には冷水を混合することによ
って温度を下げ、設定温度の温水を給湯することが可能
になるものであり、また貯湯槽の温水が設定温度より少
し低い場合、冷水の混合比率を高くして温度を低下させ
た状態で昇温手段に供給して、昇温手段の下限の加熱能
力でこの温水を加熱することによって、設定温度に温水
を昇温させて給湯することが可能になるものであり、設
定温度の温水を安定して給湯することができるものであ
る。
As described above, according to the first aspect of the present invention, a hot water tank is provided with a heat exchanger for exchanging heat with water in the hot water tank to recover exhaust heat, and the hot water stored in the hot water tank is provided. In a cogeneration system in which hot water is supplied via a heating means having a variable heating capacity, between the hot water tank and the heating means, cold water can be supplied to hot water sent from the hot water tank to the heating means and mixed. Since the mixing means is provided, if the hot water in the hot water tank is higher than the set temperature, the temperature can be lowered by mixing cold water to supply hot water at the set temperature. When the temperature is slightly lower than the set temperature, the mixing ratio of the cold water is increased and the temperature is lowered and supplied to the temperature raising means, and the hot water is heated at the lower limit heating capacity of the temperature raising means to reach the set temperature. Warm up hot water and supply hot water It is intended that becomes possible, as it can be stably hot water hot water set temperature.

【0026】また請求項2の発明は、ミキシング手段と
昇温手段との間に、流水量及び水温を計測する第一の計
測手段を備え、第一の計測手段で計測された流水量及び
水温に基づいて、ミキシング手段で混合する温水と冷水
の比率を制御するようにしたので、計測された流水量及
び水温に応じて、温水と冷水の比率を正確に制御するこ
とができるものである。
According to a second aspect of the present invention, there is provided a first measuring means for measuring a flowing water amount and a water temperature between the mixing means and the temperature increasing means, wherein the flowing water amount and the water temperature measured by the first measuring means are provided. , The ratio of hot water and cold water mixed by the mixing means is controlled, so that the ratio of hot water to cold water can be accurately controlled according to the measured flowing water amount and water temperature.

【0027】また請求項3の発明は、貯湯槽とミキシン
グ手段との間に、流水量及び水温を計測する第二の計測
手段を備えると共に、ミキシング手段に給水する冷水の
流水量及び水温を計測する第三の計測手段を備え、第二
及び第三の計測手段で計測された流水量及び水温に基づ
いて、ミキシング手段で混合する温水と冷水の比率を制
御するようにしたので、計測された流水量及び水温に応
じて、温水と冷水の比率を正確に制御することができる
ものである。
According to a third aspect of the present invention, there is provided a second measuring means for measuring the amount of flowing water and the temperature of the water between the hot water tank and the mixing means, and measuring the amount of flowing water and the temperature of the cold water supplied to the mixing means. The third measuring means is provided, and the ratio of hot water and cold water mixed by the mixing means is controlled based on the amount of flowing water and the water temperature measured by the second and third measuring means. The ratio of hot water to cold water can be accurately controlled according to the amount of flowing water and the water temperature.

【0028】また請求項4の発明は、貯湯槽内に蓄えら
れた温水の温度を計測する第四の計測手段を備え、第四
の計測手段で計測された水温に基づいて、給湯開始時に
ミキシング手段で混合する温水と冷水の比率を制御する
ようにしたので、貯湯槽内の温水の温度に応じて、給湯
開始時の温水と冷水の混合比率の制御を正確に行なうこ
とができるものである。
According to a fourth aspect of the present invention, there is provided a fourth measuring means for measuring the temperature of the hot water stored in the hot water tank, and mixing at the start of hot water supply based on the water temperature measured by the fourth measuring means. Since the ratio of hot water and cold water to be mixed is controlled by the means, it is possible to accurately control the mixing ratio of hot water and cold water at the start of hot water supply according to the temperature of the hot water in the hot water storage tank. .

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

【図1】本発明の実施の形態の一例を示す概略図であ
る。
FIG. 1 is a schematic diagram showing an example of an embodiment of the present invention.

【図2】従来例を示す概略図である。FIG. 2 is a schematic diagram showing a conventional example.

【符号の説明】[Explanation of symbols]

1 貯湯槽 2 熱交換器 3 昇温手段 4 ミキシング手段 5 第一の計測手段 6 第二の計測手段 7 第三の計測手段 8 第四の計測手段 DESCRIPTION OF SYMBOLS 1 Hot water storage tank 2 Heat exchanger 3 Heating means 4 Mixing means 5 First measuring means 6 Second measuring means 7 Third measuring means 8 Fourth measuring means

───────────────────────────────────────────────────── フロントページの続き (72)発明者 安田 雄一郎 大阪府門真市大字門真1048番地松下電工株 式会社内 Fターム(参考) 3L025 AC01  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Yuichiro Yasuda 1048 Kazuma Kadoma, Kadoma-shi, Osaka Matsushita Electric Works Co., Ltd. F-term (reference) 3L025 AC01

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 貯湯槽に貯湯槽内の温水と熱交換して排
熱を回収する熱交換器を設けると共に、貯湯槽内に蓄え
られた温水を加熱能力可変の昇温手段を介して給湯する
ようにしたコージェネレーションシステムにおいて、貯
湯槽と昇温手段との間に、貯湯槽から昇温手段に送られ
る温水に冷水を給水して混合可能なミキシング手段を備
えて成ることを特徴とするコージェネレーションシステ
ム。
1. A hot water tank is provided with a heat exchanger for exchanging heat with hot water in the hot water tank to recover exhaust heat, and hot water stored in the hot water tank is supplied to the hot water tank via a heating means having a variable heating capacity. In the cogeneration system, the mixing means is provided between the hot water tank and the temperature raising means, the mixing means being capable of supplying cold water to hot water sent from the hot water tank to the temperature raising means and mixing. Cogeneration system.
【請求項2】 ミキシング手段と昇温手段との間に、流
水量及び水温を計測する第一の計測手段を備え、第一の
計測手段で計測された流水量及び水温に基づいて、ミキ
シング手段で混合する温水と冷水の比率を制御して成る
ことを特徴とする請求項1に記載のコージェネレーショ
ンシステム。
2. A method according to claim 1, further comprising: first measuring means for measuring a flowing water amount and a water temperature between the mixing means and the temperature increasing means, and the mixing means based on the flowing water amount and the water temperature measured by the first measuring means. The cogeneration system according to claim 1, wherein a ratio of hot water and cold water to be mixed is controlled.
【請求項3】 貯湯槽とミキシング手段との間に、流水
量及び水温を計測する第二の計測手段を備えると共に、
ミキシング手段に給水する冷水の流水量及び水温を計測
する第三の計測手段を備え、第二及び第三の計測手段で
計測された流水量及び水温に基づいて、ミキシング手段
で混合する温水と冷水の比率を制御して成ることを特徴
とする請求項1又は2に記載のコージェネレーションシ
ステム。
And a second measuring means for measuring a flowing water amount and a water temperature between the hot water storage tank and the mixing means,
A third measuring means for measuring a flowing water amount and a water temperature of the cold water supplied to the mixing means, and based on the flowing water amount and the water temperature measured by the second and third measuring means, hot water and cold water mixed by the mixing means. The cogeneration system according to claim 1, wherein the ratio is controlled.
【請求項4】 貯湯槽内に蓄えられた温水の温度を計測
する第四の計測手段を備え、第四の計測手段で計測され
た水温に基づいて、給湯開始時にミキシング手段で混合
する温水と冷水の比率を制御して成ることを特徴とする
請求項3に記載のコージェネレーションシステム。
And a fourth measuring means for measuring a temperature of the hot water stored in the hot water storage tank, wherein the hot water is mixed with mixing water at the start of hot water supply by mixing means based on the water temperature measured by the fourth measuring means. The cogeneration system according to claim 3, wherein the ratio of the chilled water is controlled.
JP24048899A 1999-08-26 1999-08-26 Cogeneration system Pending JP2001065975A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24048899A JP2001065975A (en) 1999-08-26 1999-08-26 Cogeneration system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24048899A JP2001065975A (en) 1999-08-26 1999-08-26 Cogeneration system

Publications (1)

Publication Number Publication Date
JP2001065975A true JP2001065975A (en) 2001-03-16

Family

ID=17060268

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24048899A Pending JP2001065975A (en) 1999-08-26 1999-08-26 Cogeneration system

Country Status (1)

Country Link
JP (1) JP2001065975A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002364919A (en) * 2001-06-07 2002-12-18 Chofu Seisakusho Co Ltd Cogeneration system
WO2003048652A1 (en) * 2001-12-03 2003-06-12 The Tokyo Electric Power Company, Incorporated Exhaust heat recovery system
JP2004163008A (en) * 2002-11-13 2004-06-10 Rinnai Corp Cogeneration system
JP2006275363A (en) * 2005-03-29 2006-10-12 Tokyo Electric Power Co Inc:The Heat pump water heater
JP2012032061A (en) * 2010-07-29 2012-02-16 Osaka Gas Co Ltd Heat supply equipment
JP2014095489A (en) * 2012-11-07 2014-05-22 Osaka Gas Co Ltd Cogeneration system, and hot-water supply facility
JP2015534032A (en) * 2012-09-28 2015-11-26 キュンドン ナビエン カンパニー リミテッドKyungdong Navien Co.,Ltd. Hot water temperature control structure of exhaust heat recovery system using three-way valve or mixing valve, and hot water temperature control structure of exhaust heat recovery system using hot water tank heat exchanger

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002364919A (en) * 2001-06-07 2002-12-18 Chofu Seisakusho Co Ltd Cogeneration system
WO2003048652A1 (en) * 2001-12-03 2003-06-12 The Tokyo Electric Power Company, Incorporated Exhaust heat recovery system
US6938417B2 (en) 2001-12-03 2005-09-06 The Tokyo Electric Power Company, Incorporated Exhaust heat recovery system
CN1333159C (en) * 2001-12-03 2007-08-22 东京电力株式会社 Exhaust heat recovery system
JP2004163008A (en) * 2002-11-13 2004-06-10 Rinnai Corp Cogeneration system
JP2006275363A (en) * 2005-03-29 2006-10-12 Tokyo Electric Power Co Inc:The Heat pump water heater
JP2012032061A (en) * 2010-07-29 2012-02-16 Osaka Gas Co Ltd Heat supply equipment
JP2015534032A (en) * 2012-09-28 2015-11-26 キュンドン ナビエン カンパニー リミテッドKyungdong Navien Co.,Ltd. Hot water temperature control structure of exhaust heat recovery system using three-way valve or mixing valve, and hot water temperature control structure of exhaust heat recovery system using hot water tank heat exchanger
JP2014095489A (en) * 2012-11-07 2014-05-22 Osaka Gas Co Ltd Cogeneration system, and hot-water supply facility

Similar Documents

Publication Publication Date Title
CA2678397C (en) Reformer system, fuel cell system, and their operation method
JP4511878B2 (en) Fuel cell system
JPH1197044A (en) Fuel cell and hot water supply cogeneration system
WO2009131010A1 (en) Method for operating indirect internal reforming solid oxide fuel cell system
JP4399553B2 (en) Fuel cell system
WO2008016257A1 (en) Fuel cell system and operating method
JP2001065976A (en) Cogeneration system
JP2001065975A (en) Cogeneration system
JP2008176943A (en) Fuel cell system
JP2889807B2 (en) Fuel cell system
JP2002042840A (en) Fuel cell type cogeneration system
JPH11223385A (en) Cogeneration system
JP5653834B2 (en) Fuel cell system
WO2009119187A1 (en) Fuel cell system and method of load following operation of the same
JP2000018718A (en) Water heater with power generation function
JP4296741B2 (en) Cogeneration system
JP4052784B2 (en) Combined heat and power fuel cell power generator and method of operating the same
JP3062219B2 (en) Heat medium heating device of fuel reformer for fuel cell
JP2006179346A (en) Fuel cell power generation system and its operation method
JP6115230B2 (en) Fuel cell system
JP2022159919A (en) Fuel cell system and fuel cell system operating method
JP2002164061A (en) Cogeneration system
JP2002008697A (en) Operation starting method of fuel cell system and its equipment
JP2012009175A (en) Fuel cell power generation system and operation method thereof
JP2006004833A (en) Front-end system of fuel cell and fuel cell system

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20050811

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050823

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20051220