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JP4381508B2 - Fuel cell system - Google Patents
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JP4381508B2 - Fuel cell system - Google Patents

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Publication number
JP4381508B2
JP4381508B2 JP17512499A JP17512499A JP4381508B2 JP 4381508 B2 JP4381508 B2 JP 4381508B2 JP 17512499 A JP17512499 A JP 17512499A JP 17512499 A JP17512499 A JP 17512499A JP 4381508 B2 JP4381508 B2 JP 4381508B2
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Japan
Prior art keywords
fuel cell
fuel
voltage
cell system
reformed gas
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JP17512499A
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Japanese (ja)
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JP2001006706A (en
Inventor
範行 山鹿
幹夫 品川
淳治 安達
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Panasonic Corp
Panasonic Electric Works Co Ltd
Panasonic Holdings Corp
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Panasonic Corp
Matsushita Electric Industrial Co Ltd
Matsushita Electric Works Ltd
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    • 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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Description

【0001】
【発明の属する技術分野】
本発明は燃料電池システムに関し、具体的には、燃料極と酸素極を対としたセルを複数有する燃料電池本体を備える燃料電池システムに関するものである。
【0002】
【従来の技術】
燃料電池としては、リン酸型燃料電池、固体高分子電解質型燃料電池が知られている。これら燃料電池は、燃料電池本体の燃料極に還元剤として水素に富んだガスを供給し、酸素極に酸化剤として空気中の酸素を導入し、この一対の電極間で電気化学反応に基づく発電を行うものである。上記水素に富んだガスは、改質器で原燃料と水成分を反応して作製される。この改質ガスは、原燃料に天然ガス、ブタン、プロパン、ナフサ等の化石燃料を用い水蒸気改質したもの、原燃料にメタノール等のアルコール類を用い水蒸気改質したものが利用されており、上記改質ガスはガス中にCOが数%含まれている。燃料電池の電極として用いられる白金触媒は、このCOによって被毒され易いため、上記改質ガス中のCO濃度を低減する必要がある。
【0003】
そこで、運転を190℃程度で行なうリン酸型燃料電池では、化石燃料を原燃料とする場合、改質器の後段に炭素変成器を連結し、改質ガス中のCOを酸化しCO2 に変換し、CO濃度を1%程度に低減したり、メタノールを原燃料とする場合、運転温度や水蒸気と燃料の比を調整することでCO濃度を1%程度に低減することが知られている。
【0004】
【発明が解決しようとする課題】
一方、80℃程度の低温で運転する固体高分子電解質型燃料電池では、白金触媒の被毒を防ぐために、上記COの濃度を数十ppm以下と大幅に低減する必要があり、各種燃料電池システムが提案されている(例えば、特開平9−199154号等)。これらの方法は、定常運転の際は、改質ガス中のCO濃度は、数十ppm以下に維持することができるが、起動時等の急激な負荷変動が生じた際に、十分対処できない場合があり、上記COの濃度が高いと、発電能力が低下し、燃料電池システムを破損する恐れがある。
【0005】
このために、改質ガス中のCO濃度を検知し、COの濃度が所定以下となった際に、燃料電池システムに方策をとる必要がある。CO濃度検知装置として、半導体方式、電解型の電気方式、及び、赤外等の光学方式の検知装置が汎用されているが、上記半導体方式、及び、電気方式の検知装置は、数百ppmレベルのCOを検知することが難しく、上記光学方式の検知装置は、装置が極端に大型になり実用的に不向きである。
【0006】
本発明は上記の事情に鑑みてなされたもので、その目的とするところは、急激な負荷変動が生じた際においても、容易に改質ガス中のCOの濃度を検知することができる燃料電池システムを提供することにある。
【0007】
さらに、本発明の他の目的とするところは、改質ガス中のCO濃度が高くなっても、装置が破損を未然に防ぐことのできる燃料電池システムを提供することにある。
【0008】
【課題を解決するための手段】
本発明の請求項1に係る燃料電池システムは、
原燃料を改質して水素に富む改質ガスを作製する改質器と、上記改質ガス中の水素が導入される燃料極と酸素が導入される酸素極を対としたセルを複数有する燃料電池本体とを備える燃料電池システムであって、
上記セルのうち少なくとも一つのセルの電圧がCO濃度に応じて低下するセルであり、 該セルがこのセルの電圧を検知する電圧検知装置を備え
上記電圧検知装置により検知された電圧値が、上記改質ガス中のCO濃度の増加による上記燃料電池システムの破損を未然に防ぐために上記原燃料の供給の遮断が必要な電圧値以下に低下した際に、上記遮断を行う原燃料遮断手段を備えることを特徴とする。
【0011】
本発明の請求項に係る燃料電池システムは、請求項1記載の燃料電池システムにおいて、上記電圧検知装置により検知された電圧値が所定以下に低下した際に、上記燃料電池本体の負荷回路を遮断する遮断回路を備えることを特徴とする。
【0014】
【発明の実施の形態】
以下に本発明を詳細に説明する。
【0015】
図1は本発明に関連する発明の燃料電池システムの実施の形態の一例を示すものである。本発明の燃料電池システムは、改質器1と、複数のセル3を有する燃料電池本体2を備える。上記改質器1は、原燃料と水成分を水蒸気改質反応し、水素に富んだ改質ガスを作製する。上記原燃料としては、ブタン、プロパン、ナフサ等の化石燃料、メタノール等のアルコール類が挙げられるが、一般に市販されていて入手が容易な家庭用カセットコンロ等に用いられる小型ガスボンベのブタンを使用するのが好ましい。上記セル3は、固体高分子電解質膜を有し、この固体高分子電解質膜の一方に燃料極を、他方に酸素極を備え、上記燃料極に還元剤として上記水素に富んだ改質ガスを供給し、上記酸素極に酸化剤として空気中の酸素を導入し、この一対の電極間で電気化学反応に基づく発電が行われる。上記燃料電池本体2は、これらセル3を複数有するものである。
【0016】
本発明においては、上記セル3のうち少なくとも一つのセル3aに、このセル3aの電圧を検知する電圧検知装置4を備える。セル3の電位は、図6に示す如く、CO濃度に応じて電圧が低下する。例えば、CO濃度が50ppmの状態から急激に100ppmに高まった場合、セル3の電位は、1分間(符号ab間)で0.6V(符号c)から0.55V(符号d)に低下する。したがって、この電圧の低下の度合いを検知すれば、上記改質ガス中のCO濃度を検知することが可能である。本発明は、上記セル3aは電圧検知装置4を備えているので、容易に改質ガス中のCOの濃度を検知することができるため、急激な負荷の変動に対応することができる。
【0017】
次に、本発明に関連する発明の燃料電池システムについて説明する。図2は本発明に関連する発明の燃料電池システムの実施の形態の一例を示すものである。
上記燃料電池システムと異なる点についてのみ説明する。本発明においては、図2に示す如く、上記燃料電池本体2と分離して、セル3bが設置され、このセル3bに、セル3bの電圧を検知する電圧検知装置4を備える。上記セル3bの電圧を検知するためであれば、燃料電池本体2のセル3のような大きさを必要としない。したがって、電圧検知装置4を備える小さなセル3bを分離して設置することで、燃料電池システムの小型化を図ることができる。上記と同様に、本発明は、上記セル3bは電圧検知装置4を備えているので、容易に改質ガス中のCOの濃度を検知することができる。その結果、急激な負荷の変動に対応することができる。
【0018】
上記急激な負荷の変動に際し、警告ブザー、警告ランプ等により報知することで、手動で対応してもよいし、自動で対応してもよい。次に、自動で対応する一例を説明する。
図3は本発明の実施の形態の一例を示すものである。図3に示す如く、本発明は、上記セル3aの電圧検知装置4の信号を受ける判定手段5を備えると共に、この判定手段5からの信号に基づいて、原燃料の供給路6に、原燃料の供給を遮断する原燃料遮断手段7、及び、上記燃料電池本体2の負荷回路8に、この負荷回路8を遮断する遮断回路9を備える。
【0019】
上記判定手段5は、電圧検知装置4の信号を受け、セル3aの電圧値を検知し、この電圧値が所定以下に低下したか否かを判定する。セル3aの電圧値が所定の電圧値より低下すれば、改質ガス中のCO濃度が所定以上に含まれていることになるので、改質ガス中のCO濃度が所定以上に達したか否かを判定することになる。この所定の電圧値としては、例えば、CO濃度500ppm以上となる電圧を設定しておくとよい。また、燃料電池の性能に応じて、100〜1000ppmの範囲で設定してもよい。
【0020】
上記原燃料遮断手段7としては、遮断弁等が挙げられる。上記判定手段5と原燃料遮断手段7は電気回路10で接続されており、セル3aの電圧値が所定以下に低下したことを検知した際に、上記判定手段5から信号が送信され、原燃料の供給を遮断する。また、セル3aの電圧値が所定以下に低下したことを検知した際に、上記負荷回路8に備えた遮断回路9へも、上記判定手段5から信号が送信され、上記遮断回路9が作動して負荷回路8を遮断する。
【0021】
図4に示す燃料電池システムは、燃料電池本体2から分離した上記セル3bの電圧検知装置4の信号を受ける判定手段5を備えると共に、この判定手段5からの信号に基づいて、原燃料の供給路6に、原燃料の供給を遮断する原燃料遮断手段7、及び、上記燃料電池本体2の負荷回路8に、この負荷回路8を遮断する遮断回路9を備える。上記判定手段5、上記原燃料遮断手段7、及び、遮断回路9は、上述した燃料電池システムと同様の機能を有する。
【0022】
図5は、本発明に関連する発明の実施の形態の一例を示すものである。図5に示す如く、本発明は、上記改質ガス中のCOを低減するCO低減装置11を、上記改質器と燃料電池本体の間に備える。上記CO低減装置11としては、例えば、上記改質ガスに空気を混入させる手段が挙げられる。改質ガス中に数%程度の空気を混合して白金触媒と接触させ燃焼させれば、COが低減する。混合する空気量としては、空気のCO濃度が1%程度であるから、5%程度混合させれば、CO濃度が下がり、過度的な場合でも10%程度混合で充分である。上記CO低減装置11は、改質ガスと、空気の混合比率を調整する機能を有することが望ましい。上記判定手段5とCO低減装置11は電気回路12で接続されており、セル3aの電圧値が所定以下に低下したことを検知した際に、上記判定手段5から信号が送信され、改質ガスに混合される空気の量を増加させる。
【0023】
【発明の効果】
本発明の請求項1に係る燃料電池システムは、セルの電圧値が、改質ガス中のCO濃度の増加による燃料電池システムの破損を未然に防ぐために原燃料の供給の遮断が必要な電圧値以下に低下した際に、原燃料の供給を遮断する原燃料遮断手段を備えるので、改質ガス中のCO濃度が高くなっても、装置が破損を未然に防ぐことができる。
【0026】
さらに、本発明の請求項に係る燃料電池システムは、セルの電圧値が所定以下に低下した際に、燃料電池本体の負荷回路を遮断する手段遮断回路を備えるので、改質ガス中のCO濃度が高くなっても、装置が破損を未然に防ぐことができる。
【図面の簡単な説明】
【図1】 本発明に関連する発明の実施の形態の一例を示す概略図である。
【図2】 本発明に関連する発明の実施の形態の他の一例を示す概略図である。
【図3】 本発明の実施の形態の一例を示す概略図である。
【図4】 本発明に関連する発明の実施の形態の他の一例を示す概略図である。
【図5】 本発明に関連する発明の実施の形態の他の一例を示す概略図である。
【図6】 セルの電圧とCO濃度を示す説明図である。
【符号の説明】
1 改質器
2 燃料電池本体
3,3a,3b セル
4 電圧検知装置
5 判定手段
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a fuel cell system, and more particularly to a fuel cell system including a fuel cell body having a plurality of cells each having a fuel electrode and an oxygen electrode as a pair.
[0002]
[Prior art]
Known fuel cells include phosphoric acid fuel cells and solid polymer electrolyte fuel cells. These fuel cells supply hydrogen-rich gas as a reducing agent to the fuel electrode of the fuel cell body, introduce oxygen in the air as an oxidant to the oxygen electrode, and generate electricity based on an electrochemical reaction between the pair of electrodes. Is to do. The hydrogen-rich gas is produced by reacting raw fuel and water components in a reformer. This reformed gas is steam reformed using fossil fuels such as natural gas, butane, propane and naphtha as raw fuel, and steam reformed using alcohols such as methanol as raw fuel. The reformed gas contains several percent of CO in the gas. Since the platinum catalyst used as an electrode of the fuel cell is easily poisoned by this CO, it is necessary to reduce the CO concentration in the reformed gas.
[0003]
Therefore, in a phosphoric acid fuel cell that operates at about 190 ° C., when fossil fuel is used as the raw fuel, a carbon converter is connected to the rear stage of the reformer, and CO in the reformed gas is oxidized to CO 2 . In the case of conversion and reducing the CO concentration to about 1% or using methanol as the raw fuel, it is known to reduce the CO concentration to about 1% by adjusting the operating temperature or the ratio of water vapor to fuel. .
[0004]
[Problems to be solved by the invention]
On the other hand, in a solid polymer electrolyte fuel cell operating at a low temperature of about 80 ° C., in order to prevent poisoning of the platinum catalyst, it is necessary to greatly reduce the CO concentration to several tens of ppm or less. Have been proposed (for example, JP-A-9-199154). In these methods, the CO concentration in the reformed gas can be maintained at several tens of ppm or less during steady operation, but it cannot be adequately dealt with when sudden load fluctuations occur during startup, etc. When the concentration of CO is high, the power generation capacity is reduced and the fuel cell system may be damaged.
[0005]
For this reason, it is necessary to take measures for the fuel cell system when the CO concentration in the reformed gas is detected and the CO concentration falls below a predetermined level. As the CO concentration detection device, semiconductor type, electrolytic type electric type, and optical type detection devices such as infrared are widely used. However, the above-mentioned semiconductor type and electric type detection devices have a level of several hundred ppm. It is difficult to detect CO, and the above-described optical detection device is unsuitable for practical use because the device becomes extremely large.
[0006]
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a fuel cell that can easily detect the concentration of CO in the reformed gas even when a sudden load fluctuation occurs. To provide a system.
[0007]
Furthermore, another object of the present invention is to provide a fuel cell system in which the apparatus can be prevented from being damaged even if the CO concentration in the reformed gas becomes high.
[0008]
[Means for Solving the Problems]
A fuel cell system according to claim 1 of the present invention includes:
A reformer that reforms raw fuel to produce a reformed gas rich in hydrogen, and a plurality of cells each having a fuel electrode into which hydrogen in the reformed gas is introduced and an oxygen electrode into which oxygen is introduced. A fuel cell system comprising a fuel cell main body,
A cell in which the voltage of at least one of the cells decreases according to the CO concentration, and the cell includes a voltage detection device that detects the voltage of the cell ,
The voltage value detected by the voltage detection device has dropped below the voltage value necessary to shut off the supply of the raw fuel in order to prevent damage to the fuel cell system due to an increase in CO concentration in the reformed gas. In this case, a raw fuel cutoff means for performing the cutoff is provided .
[0011]
The fuel cell system according to claim 2 of the present invention is the fuel cell system according to claim 1, wherein when the voltage value detected by the voltage detection device falls below a predetermined value, the load circuit of the fuel cell main body is It is provided with the interruption | blocking circuit which interrupts | blocks.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
The present invention is described in detail below.
[0015]
FIG. 1 shows an example of an embodiment of a fuel cell system according to the present invention. The fuel cell system of the present invention includes a reformer 1 and a fuel cell main body 2 having a plurality of cells 3. The reformer 1 performs a steam reforming reaction between raw fuel and water components to produce a reformed gas rich in hydrogen. Examples of the raw fuel include fossil fuels such as butane, propane, and naphtha, and alcohols such as methanol, but use a butane of a small gas cylinder that is generally available on a commercially available cassette stove or the like. Is preferred. The cell 3 has a solid polymer electrolyte membrane, one of the solid polymer electrolyte membranes has a fuel electrode, the other has an oxygen electrode, and the fuel electrode contains the reformed gas rich in hydrogen as a reducing agent. Then, oxygen in the air is introduced as an oxidant into the oxygen electrode, and power generation based on an electrochemical reaction is performed between the pair of electrodes. Upper Ki燃 charge battery body 2 are those having a plurality of these cells 3.
[0016]
In the present invention, at least one cell 3a among the cells 3 is provided with a voltage detection device 4 for detecting the voltage of the cell 3a. As shown in FIG. 6, the voltage of the cell 3 decreases according to the CO concentration. For example, when the CO concentration suddenly increases from 100 ppm to 100 ppm, the potential of the cell 3 decreases from 0.6 V (symbol c) to 0.55 V (symbol d) in 1 minute (between codes ab). Therefore, the CO concentration in the reformed gas can be detected by detecting the degree of voltage drop. In the present invention, since the cell 3a includes the voltage detection device 4, the concentration of CO in the reformed gas can be easily detected, so that it is possible to cope with a sudden load fluctuation.
[0017]
Next, the fuel cell system of the invention related to the present invention will be described. FIG. 2 shows an example of an embodiment of a fuel cell system according to the present invention.
Only differences from the fuel cell system will be described. In the present invention, as shown in FIG. 2, a cell 3b is installed separately from the fuel cell main body 2, and the cell 3b includes a voltage detection device 4 for detecting the voltage of the cell 3b. In order to detect the voltage of the cell 3b, the size of the cell 3 of the fuel cell main body 2 is not required. Therefore, the fuel cell system can be reduced in size by separating and installing the small cells 3b including the voltage detection device 4. Similarly to the above, in the present invention, since the cell 3b includes the voltage detection device 4, the concentration of CO in the reformed gas can be easily detected. As a result, it is possible to cope with a sudden load fluctuation.
[0018]
In the case of a sudden change in load, a warning buzzer, a warning lamp, or the like may be used to respond manually or automatically. Next, an example of automatically handling will be described.
FIG. 3 shows an example of an embodiment of the present invention. As shown in FIG. 3, the present invention includes a determination unit 5 that receives a signal from the voltage detection device 4 of the cell 3 a and, based on the signal from the determination unit 5, supplies the raw fuel to the raw fuel supply path 6. The raw fuel shutoff means 7 for shutting off the supply of fuel and the load circuit 8 of the fuel cell main body 2 are provided with a shutoff circuit 9 for shutting off the load circuit 8.
[0019]
The determination means 5 receives a signal from the voltage detection device 4, detects the voltage value of the cell 3a, and determines whether or not the voltage value has decreased below a predetermined value. If the voltage value of the cell 3a falls below a predetermined voltage value, the CO concentration in the reformed gas is contained above a predetermined value, so whether or not the CO concentration in the reformed gas has reached a predetermined value or more. It will be determined. As this predetermined voltage value, for example, a voltage with a CO concentration of 500 ppm or more may be set. Moreover, you may set in the range of 100-1000 ppm according to the performance of a fuel cell.
[0020]
An example of the raw fuel cutoff means 7 is a cutoff valve. The determination means 5 and the raw fuel cutoff means 7 are connected by an electric circuit 10, and when it is detected that the voltage value of the cell 3a has dropped below a predetermined value, a signal is transmitted from the determination means 5 and the raw fuel is Shut off the supply. Further, when it is detected that the voltage value of the cell 3a has dropped below a predetermined value, a signal is transmitted from the determination means 5 to the cutoff circuit 9 provided in the load circuit 8, and the cutoff circuit 9 is activated. The load circuit 8 is shut off.
[0021]
The fuel cell system shown in FIG. 4 includes determination means 5 that receives a signal from the voltage detection device 4 of the cell 3b separated from the fuel cell main body 2, and supplies raw fuel based on the signal from the determination means 5. The path 6 is provided with a raw fuel cutoff means 7 for cutting off the supply of raw fuel, and a load circuit 8 of the fuel cell main body 2 with a cut-off circuit 9 for cutting off the load circuit 8. The determination means 5, the raw fuel cutoff means 7, and the cutoff circuit 9 have the same functions as the fuel cell system described above.
[0022]
FIG. 5 shows an example of an embodiment of the invention related to the present invention. As shown in FIG. 5, the present invention includes a CO reduction device 11 for reducing CO in the reformed gas between the reformer and the fuel cell body. Examples of the CO reduction device 11 include means for mixing air into the reformed gas. If about several percent of air is mixed in the reformed gas and brought into contact with the platinum catalyst and burned, CO is reduced. As the amount of air to be mixed, since the CO concentration of air is about 1%, if it is mixed about 5%, the CO concentration decreases, and even if it is excessive, mixing about 10% is sufficient. The CO reduction device 11 desirably has a function of adjusting the mixing ratio of the reformed gas and air. The determination means 5 and the CO reduction device 11 are connected by an electric circuit 12, and when it is detected that the voltage value of the cell 3a has dropped below a predetermined value, a signal is transmitted from the determination means 5 and the reformed gas Increase the amount of air mixed in.
[0023]
【The invention's effect】
In the fuel cell system according to claim 1 of the present invention, the voltage value of the cell is a voltage value that needs to cut off the supply of raw fuel in order to prevent damage to the fuel cell system due to an increase in the CO concentration in the reformed gas. Since the raw fuel supply means for cutting off the supply of the raw fuel when it is reduced below is provided, even if the CO concentration in the reformed gas becomes high, the apparatus can be prevented from being damaged.
[0026]
The fuel cell system according to claim 2 of the present invention, when the voltage value of cell Le drops below a predetermined value, so comprises means interrupting circuit for interrupting the load circuit of the fuel cell body, the reformed gas Even if the CO concentration increases, the apparatus can be prevented from being damaged.
[Brief description of the drawings]
FIG. 1 is a schematic diagram showing an example of an embodiment of the invention related to the present invention.
FIG. 2 is a schematic view showing another example of the embodiment of the invention related to the present invention.
FIG. 3 is a schematic diagram showing an example of an embodiment of the present invention.
FIG. 4 is a schematic view showing another example of the embodiment of the invention related to the present invention.
FIG. 5 is a schematic view showing another example of the embodiment of the invention related to the present invention.
FIG. 6 is an explanatory diagram showing cell voltage and CO concentration.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Reformer 2 Fuel cell main body 3, 3a, 3b Cell 4 Voltage detector 5 Determination means

Claims (2)

原燃料を改質して水素に富む改質ガスを作製する改質器と、上記改質ガス中の水素が導入される燃料極と酸素が導入される酸素極を対としたセルを複数有する燃料電池本体とを備える燃料電池システムであって、
上記セルのうち少なくとも一つのセルの電圧がCO濃度に応じて低下するセルであり、
該セルがこのセルの電圧を検知する電圧検知装置を備え、
上記電圧検知装置により検知された電圧値が、上記改質ガス中のCO濃度の増加による上記燃料電池システムの破損を未然に防ぐために上記原燃料の供給の遮断が必要な電圧値以下に低下した際に、上記遮断を行う原燃料遮断手段を備えることを特徴とする燃料電池システム。
A reformer that reforms raw fuel to produce a reformed gas rich in hydrogen, and a plurality of cells each having a fuel electrode into which hydrogen in the reformed gas is introduced and an oxygen electrode into which oxygen is introduced. A fuel cell system comprising a fuel cell main body,
A cell in which the voltage of at least one of the cells decreases according to the CO concentration;
E Bei voltage detecting device in which the cell detects the voltage of the cell,
The voltage value detected by the voltage detection device has dropped below the voltage value necessary to shut off the supply of the raw fuel in order to prevent damage to the fuel cell system due to an increase in CO concentration in the reformed gas. when the fuel cell system characterized Rukoto comprises a raw fuel cutoff means for performing the blocking.
上記電圧検知装置により検知された電圧値が所定以下に低下した際に、上記燃料電池本体の負荷回路を遮断する遮断回路を備えることを特徴とする請求項記載の燃料電池システム。When the voltage value detected by the voltage detection device has dropped below a predetermined value, the fuel cell system according to claim 1, characterized in that it comprises a blocking circuit for blocking the load circuit of the fuel cell body.
JP17512499A 1999-06-22 1999-06-22 Fuel cell system Expired - Lifetime JP4381508B2 (en)

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JP2003077506A (en) * 2001-08-30 2003-03-14 Nippon Soken Inc Fuel cell system
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JP2005044687A (en) * 2003-07-24 2005-02-17 Matsushita Electric Ind Co Ltd Control device for fuel cell system
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