JP3976575B2 - Fuel cell power generation system - Google Patents

Fuel cell power generation system Download PDF

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Publication number
JP3976575B2
JP3976575B2 JP2002020357A JP2002020357A JP3976575B2 JP 3976575 B2 JP3976575 B2 JP 3976575B2 JP 2002020357 A JP2002020357 A JP 2002020357A JP 2002020357 A JP2002020357 A JP 2002020357A JP 3976575 B2 JP3976575 B2 JP 3976575B2
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Japan
Prior art keywords
fuel cell
heat exchanger
circulation path
power generation
generation system
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JP2002020357A
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JP2003223913A (en
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博和 井崎
龍次 畑山
丈俊 黄木
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Sanyo Electric Co Ltd
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Sanyo Electric Co Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D18/00Small-scale combined heat and power [CHP] generation systems specially adapted for domestic heating, space heating or domestic hot-water supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2101/00Electric generators of small-scale CHP systems
    • F24D2101/30Fuel cells
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2103/00Thermal aspects of small-scale CHP systems
    • F24D2103/10Small-scale CHP systems characterised by their heat recovery units
    • F24D2103/13Small-scale CHP systems characterised by their heat recovery units characterised by their heat exchangers
    • 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

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Fuel Cell (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、燃料電池により発電する燃料電池発電システムであって、特に起動時における燃料電池の昇温手段に関する。
【0002】
【従来の技術】
燃料電池発電システムは、通常図2のように炭化水素系の原燃料を燃料改質装置1で水素主体の改質ガスに改質し、この改質ガスを燃料として燃料電池2のアノード(燃料極)に供給すると共に、空気を酸化剤ガスとしてカソード(空気極)に供給し、固体高分子膜等の電解質を介して電気化学反応が生じることにより発電するものである。
【0003】
燃料電池2は、適正な運転温度(例えば固体高分子型燃料電池の場合は約80℃)が定められており、起動時にはできるだけ早く運転温度まで昇温させることが要求される。このため、従来は第1切換弁3を閉じると共に、第2切換弁4を開けて改質ガスをPGバーナ5に導入して燃焼させ、その燃焼排ガスを利用して熱交換器6を介して水を温め、この温水を燃料電池2に供給して昇温するようにしている。
【0004】
【発明が解決しようとする課題】
上記の燃料電池昇温手段によると、燃料電池2が適正な運転温度になるまでにかなり長い時間を要する問題があった。これを解決するために、燃料電池2から排出される温水を熱交換器6に戻す循環経路を形成し、熱交換器6での昇温効率を高めることで燃料電池2を早期に運転温度まで昇温させることが試みられた。しかしながら、温水を循環使用すると温水中の溶存酸素が気泡となり、循環経路に設けるポンプの性能が低下し、送水制御に支障を来たす問題が生じた。
【0005】
本発明は、このような従来の問題を解決するためになされ、温水を循環させて燃料電池を昇温する場合に、温水中に生じる気泡を排除できるようにした燃料電池発電システムを提供することを目的とする。
【0006】
【課題を解決するための手段】
この目的を解決するための本発明の手段は、請求項1に記載したように、起動時に燃料改質装置で改質した改質ガスをPGバーナで燃焼し、その燃焼排ガスにより熱交換器を介して温めた温水を循環させて燃料電池を昇温するように構成した燃料電池発電システムにおいて、前記熱交換器から燃料電池に通じると共に、燃料電池から熱交換器に戻る循環経路が形成され、この循環経路における熱交換器より上流側で且つ循環経路に設けられたポンプより下流側に空気抜き弁を設けたことを特徴とする燃料電池発電システムを要旨とする。
又、請求項2のように、前記循環経路における燃料電池より下流側に切換弁を介して分岐路を設け、この分岐路を貯湯タンクに接続したことを特徴とするものである。
【0007】
本発明では、燃料電池を昇温する温水の循環経路における熱交換器より上流側で且つ循環経路に設けられたポンプより下流側に空気抜き弁を設けたので、温水中に生じる気泡を排除し、これにより循環経路に設けるポンプの性能及び送水制御を良好に保持することができる。又、循環経路における燃料電池より下流側に切換弁を介して分岐路を設け、この分岐路を貯湯タンクに接続したので、燃料電池が運転温度まで昇温したら、循環経路の切換弁を切り換えて温水を分岐路に流し、貯湯タンクに送り込むことができる。
【0008】
【発明の実施の形態】
次に、本発明に係る燃料電池発電システムの実施形態について、添付図面を参照しながら説明する。ここで、従来と同一部材は前記と同じ符号を付ける。
図1において、1は燃料改質装置であり、図示は省略したが改質器とCO変成器とCO除去器とから構成され、都市ガス等の原燃料を水素主体の改質ガスに改質する。即ち、脱硫後の原燃料を改質器で水蒸気改質し、次いでCO変成器で改質ガス中の大部分のCOをCOに変成し、更にCO除去器で選択酸化してCO濃度を低減する。
【0009】
改質器に関連して改質器バーナ1aが設けられ、起動時にはこの改質器バーナ1aに原燃料を供給して燃焼させることで改質器の触媒を昇温させる。燃料電池2の運転時には、アノードから排出される未反応改質ガスを改質器バーナ1aに供給して燃焼させる。燃焼に必要な空気はファン(図略)により改質器バーナ1aに供給される。
【0010】
燃料改質装置1で改質される改質ガスは、起動時には未だ安定していないため前記のように第1切換弁3を閉じて燃料電池2には供給せず、第2切換弁4を開いてPGバーナ5に供給して燃焼する。このPGバーナ5での燃焼排ガスを利用して熱交換器6により温水を作り、この温水を燃料電池2に供給することで燃料電池2を運転温度まで昇温する。
【0011】
燃料電池2を効率良く昇温させるため、熱交換器6から燃料電池2に通じると共に、燃料電池2から熱交換器6に戻る循環経路7が形成されている。この循環経路7において、熱交換器6より上流側には空気抜き弁8が設けられ、第3切換弁9を介して水供給路10が接続され、燃料電池2より下流側には第4切換弁11を介して分岐路12が設けられ、この分岐路12は貯湯タンク13に接続されている。又、循環経路7の要所にはポンプ14が設けられる。
【0012】
熱交換器6で温められた温水は、循環経路7を循環しながら燃料電池2を短時間で昇温させる。循環する温水も徐々に高温になり、温水中に含まれている溶存酸素が気泡となって混入する現象が生じるが、循環経路7中には前記のように空気抜き弁8が設けられていることから温水中の気泡は排出される。これにより、温水を熱交換器6に送り込むポンプ14が気泡によって阻害されることはなく、ポンプ性能の低下を来たしたり、或は送水制御に支障を来たすようなことがなくなる。
【0013】
燃料電池2が運転温度まで昇温した時点で、第4切換弁11を切り換えて温水を分岐路12側に誘導し、貯湯タンク13内に流入させる。燃料改質装置1での改質ガスが安定すると、第2切換弁4が閉じてPGバーナ5への改質ガス供給が停止され、同時に第1切換弁3が開いて燃料電池2のアノードへの改質ガス供給が開始する。そして、燃料電池2のカソードには反応空気が供給されて燃料電池2の運転段階に入る。
【0014】
【発明の効果】
以上説明したように、本発明は、燃料電池発電システムにおいて、起動時にPGバーナで燃焼した燃焼排ガスを利用し熱交換器を介して温水を作り、この温水で燃料電池を所定の温度まで昇温する場合において、前記熱交換器から燃料電池に通じると共に、燃料電池から熱交換器に戻る循環経路が形成され、この循環経路における熱交換器より上流側で且つ循環経路に設けられたポンプより下流側に空気抜き弁を設けたので、温水中に発生する溶存酸素の気泡を排除することができる。これにより、循環経路に設けられたポンプの性能及び送水制御を良好に保持し、循環温水による燃料電池の昇温を効率良く行うことができ、この結果電池昇温時間を短縮する効果が得られる。又、循環経路における燃料電池より下流側に切換弁を介して分岐路を設け、この分岐路を貯湯タンクに接続したので、燃料電池の昇温後の温水を貯湯タンクに送り込むことで、熱効率を高めることができる。
【図面の簡単な説明】
【図1】本発明に係る燃料電池発電システムの要部を示す説明図
【図2】従来の燃料電池発電システムの要部を示す説明図
【符号の説明】
1…燃料改質装置
2…燃料電池
3…第1切換弁
4…第2切換弁
5…PGバーナ
6…熱交換器
7…循環経路
8…空気抜き弁
9…第3切換弁
10…水供給路
11…第4切換弁
12…分岐路
13…貯湯タンク
14…ポンプ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a fuel cell power generation system that generates power using a fuel cell, and more particularly to a temperature raising means for a fuel cell at the time of startup.
[0002]
[Prior art]
As shown in FIG. 2, the fuel cell power generation system generally reforms a hydrocarbon-based raw fuel into a hydrogen-based reformed gas by the fuel reformer 1, and uses the reformed gas as fuel for the anode (fuel). In addition, the air is supplied to the cathode (air electrode) as an oxidant gas, and electricity is generated by an electrochemical reaction via an electrolyte such as a solid polymer film.
[0003]
The fuel cell 2 has an appropriate operating temperature (for example, about 80 ° C. in the case of a polymer electrolyte fuel cell), and is required to be raised to the operating temperature as soon as possible at the time of startup. For this reason, conventionally, the first switching valve 3 is closed and the second switching valve 4 is opened to introduce the reformed gas into the PG burner 5 for combustion, and the combustion exhaust gas is used to pass through the heat exchanger 6. The water is warmed, and the warm water is supplied to the fuel cell 2 to raise the temperature.
[0004]
[Problems to be solved by the invention]
According to the fuel cell temperature raising means, there is a problem that it takes a considerably long time for the fuel cell 2 to reach an appropriate operating temperature. In order to solve this problem, a circulation path for returning the hot water discharged from the fuel cell 2 to the heat exchanger 6 is formed, and the temperature rise efficiency in the heat exchanger 6 is increased to bring the fuel cell 2 to the operating temperature at an early stage. Attempts were made to raise the temperature. However, when hot water is circulated and used, dissolved oxygen in the hot water becomes bubbles, which deteriorates the performance of the pump provided in the circulation path and causes a problem that hinders water supply control.
[0005]
The present invention is made to solve such a conventional problem, and provides a fuel cell power generation system capable of eliminating bubbles generated in hot water when the temperature of the fuel cell is raised by circulating hot water. With the goal.
[0006]
[Means for Solving the Problems]
The means of the present invention for solving this object, as described in claim 1, combusts the reformed gas reformed by the fuel reformer at the time of start-up with a PG burner, and uses the combustion exhaust gas to install the heat exchanger. In the fuel cell power generation system configured to circulate warm water heated through the fuel cell and raise the temperature of the fuel cell, a circulation path is formed that leads from the heat exchanger to the fuel cell and returns from the fuel cell to the heat exchanger, The gist of the fuel cell power generation system is characterized in that an air vent valve is provided upstream of the heat exchanger in the circulation path and downstream of the pump provided in the circulation path .
According to a second aspect of the present invention, a branch path is provided on the downstream side of the fuel cell in the circulation path via a switching valve, and this branch path is connected to a hot water storage tank.
[0007]
In the present invention, since the fuel cell provided with the air vent valve on the downstream side of the pump provided and the circulation path upstream of the heat exchanger definitive the circulation path of the hot water to raise the temperature to eliminate the air bubbles generated in hot water As a result, the performance and water supply control of the pump provided in the circulation path can be satisfactorily maintained. In addition, a branch passage is provided downstream of the fuel cell in the circulation path via a switching valve, and this branch path is connected to the hot water storage tank. When the fuel cell is heated to the operating temperature, the switching valve of the circulation path is switched. Hot water can flow into the branch and feed into the hot water storage tank.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
Next, an embodiment of a fuel cell power generation system according to the present invention will be described with reference to the accompanying drawings. Here, the same members as those in the past are denoted by the same reference numerals.
In FIG. 1, reference numeral 1 denotes a fuel reformer, which is not shown, but is composed of a reformer, a CO converter and a CO remover, and reforms raw fuel such as city gas into reformed gas mainly composed of hydrogen. To do. That is, the raw fuel after desulfurization is steam reformed with a reformer, then most of the CO in the reformed gas is converted to CO 2 with a CO converter, and further selectively oxidized with a CO remover to reduce the CO concentration. Reduce.
[0009]
A reformer burner 1a is provided in association with the reformer, and at the time of start-up, raw fuel is supplied to the reformer burner 1a and burned to raise the temperature of the reformer catalyst. During operation of the fuel cell 2, unreacted reformed gas discharged from the anode is supplied to the reformer burner 1a and burned. Air necessary for combustion is supplied to the reformer burner 1a by a fan (not shown).
[0010]
Since the reformed gas reformed by the fuel reformer 1 is not yet stable at the time of start-up, the first switching valve 3 is closed and not supplied to the fuel cell 2 as described above. Open and supply to the PG burner 5 to burn. Using the combustion exhaust gas in the PG burner 5, warm water is produced by the heat exchanger 6, and the warm water is supplied to the fuel cell 2 to raise the temperature of the fuel cell 2 to the operating temperature.
[0011]
In order to efficiently raise the temperature of the fuel cell 2, a circulation path 7 that leads from the heat exchanger 6 to the fuel cell 2 and returns from the fuel cell 2 to the heat exchanger 6 is formed. In this circulation path 7, an air vent valve 8 is provided on the upstream side of the heat exchanger 6, a water supply path 10 is connected via a third switching valve 9, and a fourth switching valve on the downstream side of the fuel cell 2. A branch path 12 is provided via 11, and this branch path 12 is connected to a hot water storage tank 13. Further, a pump 14 is provided at a key point of the circulation path 7.
[0012]
The hot water heated by the heat exchanger 6 raises the temperature of the fuel cell 2 in a short time while circulating through the circulation path 7. Circulating warm water gradually becomes high temperature, and there is a phenomenon that dissolved oxygen contained in the warm water is mixed in as bubbles, but the circulation path 7 is provided with the air vent valve 8 as described above. Bubbles are discharged from the hot water. As a result, the pump 14 that feeds the hot water into the heat exchanger 6 is not hindered by the bubbles, and the pump performance is not deteriorated or the water supply control is not hindered.
[0013]
When the temperature of the fuel cell 2 rises to the operating temperature, the fourth switching valve 11 is switched to guide the hot water to the branch path 12 side and flow into the hot water storage tank 13. When the reformed gas in the fuel reformer 1 is stabilized, the second switching valve 4 is closed and the reformed gas supply to the PG burner 5 is stopped, and at the same time, the first switching valve 3 is opened to the anode of the fuel cell 2. The reformed gas supply starts. Then, the reaction air is supplied to the cathode of the fuel cell 2 and the fuel cell 2 enters the operation stage.
[0014]
【The invention's effect】
As described above, according to the present invention, in a fuel cell power generation system, hot water is produced through a heat exchanger using combustion exhaust gas combusted by a PG burner at start-up, and the fuel cell is heated to a predetermined temperature with this hot water. In this case, a circulation path that leads from the heat exchanger to the fuel cell and returns from the fuel cell to the heat exchanger is formed, upstream of the heat exchanger in the circulation path and downstream of the pump provided in the circulation path. Since the air vent valve is provided on the side, dissolved oxygen bubbles generated in the warm water can be eliminated. As a result, the performance and water supply control of the pump provided in the circulation path can be satisfactorily maintained, and the temperature of the fuel cell can be efficiently increased by the circulating hot water. As a result, the effect of shortening the battery temperature increase time can be obtained. . In addition, a branch path is provided downstream of the fuel cell in the circulation path via a switching valve, and this branch path is connected to the hot water storage tank. Can be increased.
[Brief description of the drawings]
FIG. 1 is an explanatory view showing a main part of a fuel cell power generation system according to the present invention. FIG. 2 is an explanatory view showing a main part of a conventional fuel cell power generation system.
DESCRIPTION OF SYMBOLS 1 ... Fuel reformer 2 ... Fuel cell 3 ... 1st switching valve 4 ... 2nd switching valve 5 ... PG burner 6 ... Heat exchanger 7 ... Circulation path 8 ... Air vent valve 9 ... 3rd switching valve 10 ... Water supply path 11 ... Fourth switching valve 12 ... Branch 13 ... Hot water storage tank 14 ... Pump

Claims (2)

起動時に燃料改質装置で改質した改質ガスをPGバーナで燃焼し、その燃焼排ガスにより熱交換器を介して温めた温水を循環させて燃料電池を昇温するように構成した燃料電池発電システムにおいて、前記熱交換器から燃料電池に通じると共に、燃料電池から熱交換器に戻る循環経路が形成され、この循環経路における熱交換器より上流側で且つ循環経路に設けられたポンプより下流側に空気抜き弁を設けたことを特徴とする燃料電池発電システム。Fuel cell power generation configured to burn the reformed gas reformed by the fuel reformer at the time of startup with a PG burner and circulate warm water heated by the combustion exhaust gas through the heat exchanger to raise the temperature of the fuel cell In the system, a circulation path leading from the heat exchanger to the fuel cell and returning from the fuel cell to the heat exchanger is formed, upstream of the heat exchanger in the circulation path and downstream of the pump provided in the circulation path. fuel cell power generation system characterized in that a vent valve. 前記循環経路における燃料電池より下流側に切換弁を介して分岐路を設け、この分岐路を貯湯タンクに接続した請求項1記載の燃料電池発電システム。  2. The fuel cell power generation system according to claim 1, wherein a branch path is provided downstream of the fuel cell in the circulation path via a switching valve, and the branch path is connected to a hot water storage tank.
JP2002020357A 2002-01-29 2002-01-29 Fuel cell power generation system Expired - Fee Related JP3976575B2 (en)

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KR100589408B1 (en) 2004-04-29 2006-06-14 삼성에스디아이 주식회사 Fuel cell system
JP4584337B2 (en) * 2006-09-26 2010-11-17 パナソニック株式会社 Fuel cell system
JP4650577B2 (en) * 2009-03-24 2011-03-16 パナソニック株式会社 Fuel cell cogeneration system
JP5187420B2 (en) * 2011-08-10 2013-04-24 パナソニック株式会社 Water filling method for fuel cell system

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