JP2001332281A - Solid polyelectrolyte fuel cell power generation system and its operation method - Google Patents

Solid polyelectrolyte fuel cell power generation system and its operation method

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Publication number
JP2001332281A
JP2001332281A JP2000153001A JP2000153001A JP2001332281A JP 2001332281 A JP2001332281 A JP 2001332281A JP 2000153001 A JP2000153001 A JP 2000153001A JP 2000153001 A JP2000153001 A JP 2000153001A JP 2001332281 A JP2001332281 A JP 2001332281A
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JP
Japan
Prior art keywords
fuel cell
air
cell power
power generator
polymer electrolyte
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.)
Granted
Application number
JP2000153001A
Other languages
Japanese (ja)
Other versions
JP4072707B2 (en
Inventor
Yoshiaki Enami
義晶 榎並
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
Original Assignee
Fuji Electric Co Ltd
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Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP2000153001A priority Critical patent/JP4072707B2/en
Publication of JP2001332281A publication Critical patent/JP2001332281A/en
Application granted granted Critical
Publication of JP4072707B2 publication Critical patent/JP4072707B2/en
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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

Abstract

PROBLEM TO BE SOLVED: To provide a solid polyelectrolyte fuel cell power generation system, capable of reasonably drying the inside of the fuel cell and preventing it from freezing during its shut-down and having a simple system composition and operating sequence, and offer its operation method. SOLUTION: The solid polyelectrolyte fuel cell power generation system is equipped with the fuel cell main body 1 in charge of power generation by supplying the hydrogen-contained fuel gas 8 to the anode electrode and by supplying the air 7 as an oxidant gas to the cathode electrode and with a humidifier 2, in charge of humidifying the solid-polyelectrolyte film by humidifying the air 7. During shut-down, the humidification of the air 7 is first stopped and then an air, without being humidified is supplied to the cathode electrode for a prescribed time to stop the operation of the fuel cell power generation system.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、固体高分子電解
質型燃料電池発電装置とその運転方法に関する。
The present invention relates to a solid polymer electrolyte fuel cell power generator and a method of operating the same.

【0002】[0002]

【従来の技術】一般に固体高分子電解質型燃料電池の最
小発電単位であるセルの構成は図6のように表わされ
る。膜電極接合体(MEA:Membrane Ele
ctrode Assembly)は、電解質膜31の
両面に貴金属(主として白金)を含む触媒層40を接合
して形成される。MEAの外側には多孔質の拡散層33
があって、反応ガスとしての燃料ガスと酸化剤ガスを通
過させると同時に、電流を外部に伝える働きをする。
2. Description of the Related Art In general, the structure of a cell which is the minimum power generation unit of a solid polymer electrolyte fuel cell is shown in FIG. Membrane Ele (MEA: Membrane Ele)
Ctrode assembly is formed by bonding a catalyst layer 40 containing a noble metal (mainly platinum) to both surfaces of the electrolyte membrane 31. A porous diffusion layer 33 is provided outside the MEA.
There is a function to transmit a current to the outside while passing a fuel gas and an oxidizing gas as reaction gases.

【0003】多孔質の拡散層33と触媒層40とを合わ
せて、燃料ガスが通流される側をアノード電極,酸化剤
ガスが通流される側をカソード電極という。また、広義
のMEAには拡散層を含めることもある。上記両電極
を、燃料ガス流路および酸化剤ガス流路を備えたセパレ
ータ32で挟むことにより、セルが構成される。このセ
ルを多数積層したものをスタックという。
[0003] Together with the porous diffusion layer 33 and the catalyst layer 40, the side through which the fuel gas flows is called the anode electrode, and the side through which the oxidizing gas flows is the cathode electrode. Further, the MEA in a broad sense may include a diffusion layer. A cell is formed by sandwiching the two electrodes between the separators 32 each having a fuel gas flow path and an oxidizing gas flow path. A stack of many of these cells is called a stack.

【0004】電解質膜にはフッ素系の高分子材料が最も
一般的に使用されている。代表的な市販の電解質膜には
NafionTM(米国・デュポン社製商品名)がある。これら
の電解質膜の特徴は、他の高分子電解質と比較してプロ
トン伝導性が高いことと、電解質膜が乾燥すると急激に
プロトン伝導性が低下することである。このため固体高
分子電解質型燃料電池では常に電解質膜を適当な含水状
態に制御することが求められる。通常は反応ガスを加湿
することによって電解質膜の乾燥を防止する。
[0004] For the electrolyte membrane, a fluorine-based polymer material is most commonly used. Typical commercially available electrolyte membranes include
There is Nafion TM (trade name, manufactured by DuPont, USA). The features of these electrolyte membranes are that they have higher proton conductivity than other polymer electrolytes, and that the proton conductivity rapidly decreases when the electrolyte membrane dries. For this reason, in a solid polymer electrolyte fuel cell, it is required to always control the electrolyte membrane to an appropriate water-containing state. Usually, drying of the electrolyte membrane is prevented by humidifying the reaction gas.

【0005】加湿のための水は生成水を回収して利用す
るか、または外部より供給する。電解質は金属イオンを
吸着するので、加湿に使用する水はイオン交換などの方
法によって金属イオンが除去されている必要がある。ま
た生成水を回収して利用するには付加的な装置が必要で
ある。
[0005] Water for humidification is obtained by collecting and using produced water or supplied from outside. Since the electrolyte adsorbs metal ions, the water used for humidification must be free of metal ions by a method such as ion exchange. Further, additional equipment is required to collect and use the generated water.

【0006】[0006]

【発明が解決しようとする課題】前述のように、固体高
分子電解質型燃料電池の電解質膜は高分子イオン交換膜
であり、運転時には湿潤状態にする必要があるため、燃
料電池に供給する反応ガスには加湿手段により水分が添
加される。また燃料電池の発電によっても水が発生す
る。固体高分子電解質型燃料電池は、運転圧力での水の
沸点以下の温度で運転されるため、これらの水分が電池
の内部で液状となって存在する場合が多い。
As described above, the electrolyte membrane of a solid polymer electrolyte fuel cell is a polymer ion exchange membrane, which must be kept wet during operation. Water is added to the gas by humidifying means. Water is also generated by the power generation of the fuel cell. Since a solid polymer electrolyte fuel cell is operated at a temperature equal to or lower than the boiling point of water at the operating pressure, such water is often present in a liquid state inside the cell.

【0007】寒冷地では、固体高分子電解質型燃料電池
の内部に残留する上記液状の水が運転停止後に凍結し、
触媒層や拡散層内部の微細構造を破壊する恐れがある。
In cold regions, the above-mentioned liquid water remaining inside the solid polymer electrolyte fuel cell freezes after the operation is stopped,
There is a possibility that the microstructure inside the catalyst layer or the diffusion layer is destroyed.

【0008】上記問題に対処するため、反応ガスとして
の燃料ガスに水を吹き込んで気液混合物を生成して加湿
するタイプの固体高分子電解質型燃料電池発電装置にお
いては、燃料電池停止時に、反応空気用ブロワとは別に
設けられた空気ポンプを備えた燃料電池内水排出手段に
より、冷却水タンクに水を回収する方式、あるいは、燃
料ガスポンプのみを継続運転させて冷却水タンクに水を
回収する方式などが提案されている(特開平9−147
892号公報参照)。
In order to cope with the above problem, in a solid polymer electrolyte fuel cell power generation apparatus of the type in which water is blown into a fuel gas as a reaction gas to generate a gas-liquid mixture and humidify the reaction gas when the fuel cell is stopped. A method of collecting water in a cooling water tank by water discharging means in a fuel cell provided with an air pump provided separately from an air blower, or collecting water in a cooling water tank by continuously operating only a fuel gas pump A method has been proposed (Japanese Unexamined Patent Publication No. 9-147).
No. 892).

【0009】しかしながら、上記特開平9−14789
2号公報に記載された方式は、全体として、システム構
成および操作手順が複雑であり、特に前記二方式の内、
前者の方式は、反応空気用ブロワとは別に空気ポンプを
設ける必要があり、その分過剰設備となる問題がある。
However, Japanese Patent Application Laid-Open No. Hei 9-14789 discloses
The system described in Japanese Patent Publication No. 2 has a complicated system configuration and operating procedure as a whole.
In the former method, it is necessary to provide an air pump separately from the reaction air blower, and there is a problem that excess equipment is required.

【0010】この発明は、上記の点に鑑みてなされたも
ので、この発明の課題は、装置構成および操作手順が簡
単で、かつ発電装置停止時において電池内部の合理的な
乾燥状態が得られる固体高分子電解質型燃料電池発電装
置とその運転方法を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above points, and it is an object of the present invention to provide an apparatus having a simple structure and operating procedure, and to obtain a reasonable dry state inside the battery when the power generator is stopped. An object of the present invention is to provide a solid polymer electrolyte fuel cell power generator and an operation method thereof.

【0011】[0011]

【課題を解決するための手段】前述の課題を解決するた
めに、この発明においては、燃料電池発電装置が外部へ
の電気出力を終了し停止状態に入る際に、ある程度の時
間だけ燃料電池本体に乾燥ガスを供給する。
In order to solve the above-mentioned problems, according to the present invention, when the fuel cell power generation device terminates the electric output to the outside and enters a stop state, the fuel cell main body has a certain period of time. Supply dry gas to

【0012】乾燥ガスとしては空気を用いるのが簡便で
ある。空気に対する加湿を停止することで電池の運転温
度では充分な乾燥効果を持ったガスが得られる。加湿を
停止する方法は加湿手段によって異なるが、加湿水の供
給を停止し、加湿装置内部の水を抜く、加湿装置をバイ
パスするといった方法がある。
It is convenient to use air as the drying gas. By stopping the humidification to the air, a gas having a sufficient drying effect can be obtained at the operating temperature of the battery. The method of stopping the humidification depends on the humidification means, but there is a method of stopping the supply of the humidification water, draining the water inside the humidification device, and bypassing the humidification device.

【0013】空気を用いた場合には燃料電池が空気の供
給装置へ電力を供給しつづけられるので、系統接続を行
わない小型の発電装置でも適用可能である。また系統接
続が行われている場合には燃料電池本体が完全に発電を
停止した状態で空気を乾燥ガスとして導入することも可
能である。
[0013] When air is used, the fuel cell keeps supplying power to the air supply device, so that it can be applied even to a small power generation device without system connection. In addition, when the system connection is made, it is possible to introduce air as a dry gas in a state where the power generation of the fuel cell body is completely stopped.

【0014】乾燥ガスを供給する時間は、乾燥ガスの流
量に応じてあらかじめ適当な値を定めることができる。
また電解質膜の乾燥による出力電圧の低下を監視するこ
とで乾燥ガスの供給時間を決めることも可能である。こ
のように乾燥時間を制限する理由は、乾燥時間が長すぎ
ると再起動に要する時間が長くなるからである。
The time for supplying the drying gas can be set to an appropriate value in advance according to the flow rate of the drying gas.
It is also possible to determine the supply time of the dry gas by monitoring a decrease in the output voltage due to the drying of the electrolyte membrane. The reason for limiting the drying time in this way is that if the drying time is too long, the time required for restarting is increased.

【0015】上記の考え方を基礎として、請求項1の発
明は、固体高分子電解質膜を挟んで配設した触媒層と多
孔質の拡散層とからなるアノード電極およびカソード電
極を有し、前記アノード電極に水素を含む燃料ガスを供
給し、前記カソード電極に酸化剤ガスとして空気を供給
することにより発電を行う燃料電池本体と、前記空気を
加湿することにより固体高分子電解質膜を加湿する加湿
装置とを備えた固体高分子電解質型燃料電池発電装置の
運転方法において、運転停止時に、まず前記空気の加湿
を停止し、その後、カソード電極に無加湿の空気を所定
時間供給した後に、燃料電池発電装置の運転を停止する
こととする。
[0015] Based on the above concept, the invention of claim 1 includes an anode electrode and a cathode electrode each comprising a catalyst layer and a porous diffusion layer disposed with a solid polymer electrolyte membrane interposed therebetween, and A fuel cell main body for generating electricity by supplying a fuel gas containing hydrogen to the electrode and supplying air as an oxidant gas to the cathode electrode, and a humidifier for humidifying the solid polymer electrolyte membrane by humidifying the air In the operation method of the solid polymer electrolyte fuel cell power generator including the above, when the operation is stopped, first the humidification of the air is stopped, and after the non-humidified air is supplied to the cathode electrode for a predetermined time, the fuel cell power generation is started. The operation of the device shall be stopped.

【0016】上記により、燃料電池停止時に、加湿を停
止した上で反応空気用ブロワを、固体高分子電解質膜の
乾燥に好ましい所定時間(例えば、3分程度)運転を継
続するのみで所期の目的を達成できるので、構成および
操作手順が簡略となる。
As described above, when the fuel cell is stopped, the humidification is stopped, and the reaction air blower is operated for a predetermined period of time (for example, about 3 minutes) which is preferable for drying the solid polymer electrolyte membrane. Since the object can be achieved, the configuration and the operation procedure are simplified.

【0017】また、電解質膜の最適乾燥状態は、前述の
ように燃料電池の出力電圧によって評価できるので、過
乾燥や無駄時間を避ける観点から請求項2の発明が好ま
しい。即ち、前記請求項1記載の燃料電池発電装置の運
転方法において、前記所定時間に代えて、カソード電極
に無加湿空気の供給を行って前記燃料電池本体を低負荷
状態で運転し、電解質膜の乾燥により燃料電池本体の出
力電圧が所定の値に低下した時点で、燃料電池発電装置
の運転を停止することとする。
Further, since the optimum drying state of the electrolyte membrane can be evaluated by the output voltage of the fuel cell as described above, the invention of claim 2 is preferable from the viewpoint of avoiding overdrying and wasted time. That is, in the operating method of the fuel cell power generator according to claim 1, the fuel cell main body is operated in a low load state by supplying non-humidified air to the cathode electrode instead of the predetermined time, and The operation of the fuel cell power generator is stopped when the output voltage of the fuel cell body drops to a predetermined value due to the drying.

【0018】さらに、上記請求項1または2の発明の方
法を実施するための固体高分子電解質型燃料電池発電装
置としては、固体高分子電解質膜を挟んで配設した触媒
層と多孔質の拡散層とからなるアノード電極およびカソ
ード電極を有し、前記アノード電極に水素を含む燃料ガ
スを供給し、前記カソード電極に酸化剤ガスとして空気
を供給することにより発電を行う燃料電池本体と、前記
空気を加湿することにより固体高分子電解質膜を加湿す
る加湿装置と、燃料電池発電装置の運転停止時に、まず
前記空気の加湿を停止し,カソード電極に無加湿空気を
所定時間供給した後にもしくは燃料電池本体の出力電圧
が所定の値に低下した時点で,燃料電池発電装置の運転
を停止する制御装置とを備えたものとする(請求項3の
発明)。
Further, a solid polymer electrolyte fuel cell power generator for carrying out the method according to the first or second aspect of the present invention includes a catalyst layer provided with a solid polymer electrolyte membrane interposed therebetween and a porous diffusion layer. A fuel cell main body having an anode electrode and a cathode electrode comprising a layer, a fuel gas containing hydrogen supplied to the anode electrode, and air supplied as an oxidant gas to the cathode electrode to generate electric power; and A humidifier for humidifying the solid polymer electrolyte membrane by humidifying the fuel cell, and when the operation of the fuel cell power generator is stopped, first humidification of the air is stopped, and after supplying non-humidified air to the cathode electrode for a predetermined time, or A control device for stopping the operation of the fuel cell power generation device when the output voltage of the main body falls to a predetermined value is provided (the invention of claim 3).

【0019】前記加湿装置の実施態様としては、下記の
請求項4ないし7の発明が好適である。即ち、まず請求
項3記載の燃料電池発電装置において、空気を加湿する
加湿装置は、加湿膜を有し、かつこの加湿膜主面の一側
に水を貯留する空間を備え、他側に空気を通流する空間
を備えたものとし、前記空気の加湿停止は、貯留された
水を排出することにより行うように構成したものとする
(請求項4の発明)。
As the embodiments of the humidifying device, the following inventions of claims 4 to 7 are preferable. That is, first, in the fuel cell power generator according to claim 3, the humidifying device for humidifying the air has a humidifying film, and has a space for storing water on one side of the main surface of the humidifying film, and the air on the other side. A space through which air flows is provided, and the humidification of the air is stopped by discharging stored water (the invention of claim 4).

【0020】また、請求項3記載の燃料電池発電装置に
おいて、空気を加湿する加湿装置は、加湿用容器に貯留
された水の中に空気を散気し、水中から脱気した空気を
燃料電池本体へ通流する構成を有し、前記空気の加湿停
止は、貯留された水を排出することにより行うように構
成したものとする(請求項5の発明)。
Further, in the fuel cell power generator according to the third aspect, the humidifying device for humidifying the air diffuses the air into the water stored in the humidifying container and removes the air deaerated from the water. It has a configuration in which the air flows into the main body, and the humidification of the air is stopped by discharging the stored water (the invention of claim 5).

【0021】さらに、請求項4または5に記載の燃料電
池発電装置において、加湿装置は、加湿膜主面の一側に
貯留する水または加湿用容器に貯留される水を、別置の
貯水タンクからポンプ手段により導入・排出入するよう
に構成してなり、さらにこのポンプ手段は、少なくとも
4つの弁からなる流通方向切替手段を備え、前記制御装
置は、燃料電池発電装置の運転停止時に、前記流通方向
切替により、貯留された水を排出するように構成したも
のとする(請求項6の発明)。
Further, in the fuel cell power generator according to claim 4 or 5, the humidifier is provided with a water storage tank separately provided with water stored on one side of the main surface of the humidifying film or water stored in the humidifying container. And the pump means comprises a flow direction switching means comprising at least four valves, and the control device, when the operation of the fuel cell power generation device is stopped, It is configured such that the stored water is discharged by switching the flow direction (the invention of claim 6).

【0022】さらにまた、請求項4または5に記載の燃
料電池発電装置において、加湿装置は、さらに、無加湿
空気を燃料電池本体へ直接通流するバイパス回路とバイ
パス回路への切替装置とを備え、前記空気の加湿停止
は、空気の通流をこのバイパス回路へ切り替えることに
より行うように構成したものとする(請求項7の発
明)。
Further, in the fuel cell power generator according to the fourth or fifth aspect, the humidifier further includes a bypass circuit for allowing non-humidified air to flow directly to the fuel cell body and a switching device for switching to the bypass circuit. The humidification of the air is stopped by switching the flow of the air to the bypass circuit (the invention of claim 7).

【0023】上記加湿装置の実施態様は、燃料電池発電
装置の容量や顧客ニーズに基づく仕様によって使い分け
られる。特に、加湿用の水を導入・排出する手段,手順
を簡略化するためには、請求項6の発明が好適である。
The embodiment of the humidifier can be properly used depending on the capacity of the fuel cell power generator and specifications based on customer needs. In particular, the invention according to claim 6 is suitable for simplifying the means and procedure for introducing and discharging humidifying water.

【0024】[0024]

【発明の実施の形態】図面に基づき、本発明の実施の形
態について以下にのべる。
Embodiments of the present invention will be described below with reference to the drawings.

【0025】図1は、この発明の実施例、特に請求項6
の発明に関わる概略システム系統図を示す。図1に示す
燃料電池発電装置は、燃料電池本体1と、この燃料電池
本体に水素リッチな改質燃料ガス8を供給する改質装置
3と、反応空気7を供給するブロワ4と、この空気を加
湿することにより固体高分子電解質膜を加湿する加湿装
置2と、燃料電池発電装置の運転停止時に、まず前記空
気の加湿を停止し,カソード電極に無加湿空気を所定時
間供給した後にもしくは燃料電池本体の出力電圧が所定
の値に低下した時点で,燃料電池発電装置の運転を停止
する制御装置20とを備える。
FIG. 1 shows an embodiment of the present invention.
1 shows a schematic system diagram according to the invention of FIG. The fuel cell power generator shown in FIG. 1 includes a fuel cell main body 1, a reformer 3 for supplying a hydrogen-rich reformed fuel gas 8 to the fuel cell main body, a blower 4 for supplying reaction air 7, A humidifier 2 for humidifying the solid polymer electrolyte membrane by humidifying the fuel cell, and when the operation of the fuel cell power generator is stopped, first, the humidification of the air is stopped, and after the non-humidified air is supplied to the cathode for a predetermined time or And a control device for stopping the operation of the fuel cell power generation device when the output voltage of the battery body drops to a predetermined value.

【0026】さらに、加湿装置2は、加湿膜主面の一側
に貯留する水または加湿用容器に貯留される水を、別置
の貯水タンク6からポンプ手段5により導入・排出入す
るように構成されており、さらにこのポンプ手段5は、
4つの弁10、11からなる流通方向切替手段を備え、
前記制御装置20は、燃料電池発電装置の運転停止時
に、前記流通方向切替により、加湿膜主面の一側に貯留
された水または加湿用容器に貯留された水を、排出する
ように構成されている。
Further, the humidifier 2 introduces and discharges water stored on one side of the main surface of the humidifying film or water stored in the humidifying container from the separately provided water tank 6 by the pump means 5. And the pump means 5 is
A flow direction switching means comprising four valves 10 and 11;
The control device 20 is configured to discharge the water stored on one side of the humidifying film main surface or the water stored in the humidifying container when the operation of the fuel cell power generation device is stopped, by switching the flow direction. ing.

【0027】図1において、通常運転時においては、燃
料電池本体1と加湿装置2の本体部21には、ポンプ手
段5によってタンク6から水が通流され、配管9を介し
還流する。ポンプ手段5は、開閉弁10(2個)と開閉
弁11(2個)とを切り替えることにより、送液方向を
逆転させることができる。即ち、開閉弁10(2個)を
開、開閉弁11(2個)を閉の状態で運転する時には、
タンク6の水が加湿装置2の本体部21に通流される。
逆に、開閉弁10(2個)を閉、開閉弁11(2個)を
開の状態で運転する時には、流れが逆方向となり、加湿
装置2の本体部21内の水は、タンク6内へ排出され
る。
In FIG. 1, during normal operation, water flows from the tank 6 to the fuel cell main body 1 and the main body 21 of the humidifier 2 by the pump means 5, and flows back through the pipe 9. The pump means 5 can reverse the liquid sending direction by switching between the on-off valves 10 (two) and the on-off valves 11 (two). That is, when operating with the on-off valves 10 (two) open and the on-off valves 11 (two) closed,
The water in the tank 6 flows through the main body 21 of the humidifier 2.
Conversely, when operating with the on-off valves 10 (two) closed and the on-off valves 11 (two) open, the flow is in the opposite direction, and the water in the main body 21 of the humidifier 2 Is discharged to

【0028】ブロワ4で供給される空気は加湿装置2で
加湿された後、燃料電池本体1を通過する。燃料ガス8
は改質装置3から燃料電池本体1を通過し、残余が再び
改質装置3に戻り燃焼し、改質反応用の熱として利用さ
れる。
The air supplied by the blower 4 is humidified by the humidifier 2 and then passes through the fuel cell body 1. Fuel gas 8
Passes through the fuel cell body 1 from the reformer 3, and the remainder returns to the reformer 3 and burns, and is used as heat for the reforming reaction.

【0029】燃料電池発電装置の停止時の動作は、例え
ば、図2のようになる。外部への電力出力を止めた後、
ポンプ手段5の送液方向を逆転させて加湿装置2の本体
内部から水を排出する。このとき燃料ガスと空気の供給
は続けられ、燃料電池本体1は低負荷で運転状態とな
る。加湿水が排出されたことで空気が乾燥状態で電池本
体に供給されるようになり、電極内部の水が排出され
る。電解質膜の乾燥により、同時に電池本体1の出力電
圧が低下する。適切な時間が経過すると(例えば3分
間)あるいは、出力電圧が所定の値に低下した時点で、
燃料ガスと空気の供給が停止され、燃料電池発電装置は
完全な停止状態に移行する。
The operation when the fuel cell power generation device is stopped is as shown in FIG. 2, for example. After stopping the power output to the outside,
Water is discharged from the inside of the main body of the humidifier 2 by reversing the liquid feeding direction of the pump means 5. At this time, the supply of the fuel gas and the air is continued, and the fuel cell main body 1 enters an operating state with a low load. By discharging the humidified water, the air is supplied to the battery body in a dry state, and the water inside the electrode is discharged. By drying the electrolyte membrane, the output voltage of the battery main body 1 is reduced at the same time. After an appropriate time has elapsed (for example, 3 minutes) or when the output voltage has dropped to a predetermined value,
The supply of fuel gas and air is stopped, and the fuel cell power generator shifts to a completely stopped state.

【0030】なお、上記実施例では、乾燥ガスを供給し
ている間、燃料電池本体1は低負荷運転状態としたが、
必ずしも電池本体が運転状態にあることを必要とするも
のではない。
In the above embodiment, the fuel cell body 1 is in the low load operation state while the dry gas is being supplied.
It does not necessarily require that the battery body be in the operating state.

【0031】次に、加湿装置の実施の形態について、装
置を概念的に示した図3ないし5により説明する。
Next, an embodiment of the humidifier will be described with reference to FIGS.

【0032】図3に示す加湿装置は、加湿膜51を挟ん
で水を貯留する空間52と空気を通流する空間53とを
備え、加湿膜51を介して空気の加湿を行うように構成
されたものを示す。貯留された水を排出することによ
り、空気の加湿は停止する。
The humidifier shown in FIG. 3 has a space 52 for storing water and a space 53 for flowing air with a humidifying film 51 interposed therebetween, and is configured to humidify the air via the humidifying film 51. Are shown. By discharging the stored water, the humidification of the air is stopped.

【0033】図4に示す加湿装置は、加湿用容器61に
貯留された水の中に空気を、散気装置62を介して散気
し、水中から脱気した空気を燃料電池本体へ通流するよ
うに構成されたものを示す。この場合も、空気の加湿停
止は、貯留された水を排出することにより行われる。
The humidifier shown in FIG. 4 diffuses air into water stored in a humidifying container 61 through a diffuser 62, and flows air deaerated from the water to the fuel cell body. Is shown. Also in this case, the humidification of the air is stopped by discharging the stored water.

【0034】図5に示す加湿装置は、図4に示す加湿装
置に、さらに、無加湿空気を燃料電池本体へ直接通流す
るバイパス回路71とバイパス回路への切替装置として
の切替弁72を備えたものを示す。空気の加湿停止は、
空気の通流をこのバイパス回路71へ切り替えることに
より行われる。なお、図3に示すものに、バイパス回路
を設けることもできる。
The humidifying device shown in FIG. 5 further includes a bypass circuit 71 for allowing non-humidified air to flow directly to the fuel cell main body and a switching valve 72 as a switching device for switching to the bypass circuit, in addition to the humidifying device shown in FIG. Are shown. Stop humidification of air
This is performed by switching the flow of air to the bypass circuit 71. Note that a bypass circuit can be provided in the configuration shown in FIG.

【0035】[0035]

【発明の効果】上記のとおり、この発明によれば、固体
高分子電解質膜を挟んで配設した触媒層と多孔質の拡散
層とからなるアノード電極およびカソード電極を有し、
前記アノード電極に水素を含む燃料ガスを供給し、前記
カソード電極に酸化剤ガスとして空気を供給することに
より発電を行う燃料電池本体と、前記空気を加湿するこ
とにより固体高分子電解質膜を加湿する加湿装置とを備
えた固体高分子電解質型燃料電池発電装置の運転方法に
おいて、運転停止時に、まず前記空気の加湿を停止し、
その後、カソード電極に無加湿の空気を所定時間供給し
た後に、燃料電池発電装置の運転を停止することとした
ので、装置構成および操作手順が簡単で、かつ発電装置
停止時において電池内部の合理的な乾燥状態が得られる
固体高分子電解質型燃料電池発電装置とその運転方法を
提供することができる。上記により、燃料電池の電極内
部に存在する過剰な水分を乾燥ガスによって蒸発させ
て、寒冷時に電極内部の凍結による構造破壊を防止する
ことができ、寒冷地での起動・停止の繰り返しによる出
力電圧の長期的な低下を抑制することが可能となる。
As described above, according to the present invention, there are provided an anode electrode and a cathode electrode each comprising a catalyst layer and a porous diffusion layer provided with a solid polymer electrolyte membrane interposed therebetween,
A fuel cell body that generates fuel by supplying a fuel gas containing hydrogen to the anode electrode and air as an oxidant gas to the cathode electrode, and humidifies the solid polymer electrolyte membrane by humidifying the air. In a method for operating a solid polymer electrolyte fuel cell power generator including a humidifier, when the operation is stopped, first stop the humidification of the air,
Thereafter, the operation of the fuel cell power generator is stopped after supplying non-humidified air to the cathode electrode for a predetermined time, so that the apparatus configuration and operation procedure are simple, and the ratio of the inside of the battery is reasonable when the power generator is stopped. It is possible to provide a solid polymer electrolyte fuel cell power generator capable of obtaining a dry state and a method of operating the same. By the above, the excess moisture present inside the electrode of the fuel cell is evaporated by the dry gas, so that the structure can be prevented from being destroyed due to freezing inside the electrode in cold weather, and the output voltage due to repeated start-stop in a cold region Can be suppressed over a long period of time.

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

【図1】この発明の燃料電池発電装置の実施例に関わる
概略システム系統図
FIG. 1 is a schematic system diagram of an embodiment of a fuel cell power generator according to the present invention.

【図2】この発明の燃料電池発電装置停止時の動作手順
の一例を示す図
FIG. 2 is a diagram showing an example of an operation procedure when the fuel cell power generator according to the present invention is stopped.

【図3】この発明の加湿膜を備えた加湿装置の概念図FIG. 3 is a conceptual diagram of a humidifying device having a humidifying film according to the present invention.

【図4】この発明の加湿用容器を備えた加湿装置の概念
FIG. 4 is a conceptual diagram of a humidifying device provided with the humidifying container of the present invention.

【図5】図4の加湿装置に対しバイパス回路を備えた加
湿装置の概念図
FIG. 5 is a conceptual diagram of a humidifier having a bypass circuit with respect to the humidifier of FIG.

【図6】固体高分子電解質型燃料電池のセルの構成を示
す斜視図
FIG. 6 is a perspective view showing a configuration of a cell of a solid polymer electrolyte fuel cell.

【符号の説明】[Explanation of symbols]

1:燃料電池本体、2:加湿装置、3:改質装置、4:
ブロワ、5:ポンプ手段、6:タンク、7:空気、8:
燃料ガス、10,11:開閉弁、20:制御装置、3
1:電解質膜、32:セパレータ、33:拡散層、4
0:触媒層、51:加湿膜、61:加湿用容器、71:
バイパス回路。
1: fuel cell body, 2: humidifier, 3: reformer, 4:
Blower, 5: pump means, 6: tank, 7: air, 8:
Fuel gas, 10, 11: open / close valve, 20: control device, 3
1: electrolyte membrane, 32: separator, 33: diffusion layer, 4
0: catalyst layer, 51: humidifying film, 61: humidifying container, 71:
Bypass circuit.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 固体高分子電解質膜を挟んで配設した触
媒層と多孔質の拡散層とからなるアノード電極およびカ
ソード電極を有し、前記アノード電極に水素を含む燃料
ガスを供給し、前記カソード電極に酸化剤ガスとして空
気を供給することにより発電を行う燃料電池本体と、前
記空気を加湿することにより固体高分子電解質膜を加湿
する加湿装置とを備えた固体高分子電解質型燃料電池発
電装置の運転方法において、運転停止時に、まず前記空
気の加湿を停止し、その後、カソード電極に無加湿の空
気を所定時間供給した後に、燃料電池発電装置の運転を
停止することを特徴とする固体高分子電解質型燃料電池
発電装置の運転方法。
An anode electrode and a cathode electrode each comprising a catalyst layer and a porous diffusion layer disposed with a solid polymer electrolyte membrane interposed therebetween, wherein a fuel gas containing hydrogen is supplied to the anode electrode; A solid polymer electrolyte fuel cell power generator comprising: a fuel cell main body that generates power by supplying air as an oxidant gas to a cathode electrode; and a humidifier that humidifies the air to humidify the solid polymer electrolyte membrane. In the operation method of the device, when the operation is stopped, first, the humidification of the air is stopped, and after the non-humidified air is supplied to the cathode electrode for a predetermined time, the operation of the fuel cell power generation device is stopped. A method for operating a polymer electrolyte fuel cell power generator.
【請求項2】 請求項1記載の燃料電池発電装置の運転
方法において、前記所定時間に代えて、カソード電極に
無加湿空気の供給を行って前記燃料電池本体を低負荷状
態で運転し、電解質膜の乾燥により燃料電池本体の出力
電圧が所定の値に低下した時点で、燃料電池発電装置の
運転を停止することを特徴とする固体高分子電解質型燃
料電池発電装置の運転方法。
2. The method of operating a fuel cell power generator according to claim 1, wherein the fuel cell main body is operated in a low load state by supplying non-humidified air to the cathode electrode instead of the predetermined time. A method for operating a solid polymer electrolyte fuel cell power generator, wherein the operation of the fuel cell power generator is stopped when the output voltage of the fuel cell body drops to a predetermined value due to drying of the membrane.
【請求項3】 固体高分子電解質膜を挟んで配設した触
媒層と多孔質の拡散層とからなるアノード電極およびカ
ソード電極を有し、前記アノード電極に水素を含む燃料
ガスを供給し、前記カソード電極に酸化剤ガスとして空
気を供給することにより発電を行う燃料電池本体と、前
記空気を加湿することにより固体高分子電解質膜を加湿
する加湿装置と、燃料電池発電装置の運転停止時に、ま
ず前記空気の加湿を停止し,カソード電極に無加湿空気
を所定時間供給した後にもしくは燃料電池本体の出力電
圧が所定の値に低下した時点で,燃料電池発電装置の運
転を停止する制御装置とを備えたことを特徴とする固体
高分子電解質型燃料電池発電装置。
3. An anode and a cathode comprising a catalyst layer and a porous diffusion layer disposed with a solid polymer electrolyte membrane interposed therebetween, and a fuel gas containing hydrogen is supplied to the anode. A fuel cell main body that generates power by supplying air as an oxidant gas to the cathode electrode, a humidifier that humidifies the solid polymer electrolyte membrane by humidifying the air, and when the operation of the fuel cell power generator is stopped, A control device for stopping the humidification of the air and stopping the operation of the fuel cell power generation device after supplying the non-humidified air to the cathode electrode for a predetermined time or when the output voltage of the fuel cell main body falls to a predetermined value. A solid polymer electrolyte fuel cell power generator, comprising:
【請求項4】 請求項3記載の燃料電池発電装置におい
て、空気を加湿する加湿装置は、加湿膜を有し、かつこ
の加湿膜主面の一側に水を貯留する空間を備え、他側に
空気を通流する空間を備えたものとし、前記空気の加湿
停止は、貯留された水を排出することにより行うように
構成したことを特徴とする固体高分子電解質型燃料電池
発電装置。
4. The fuel cell power generator according to claim 3, wherein the humidifying device for humidifying the air has a humidifying film, and has a space for storing water on one side of the main surface of the humidifying film, and the other side. A solid polymer electrolyte fuel cell power generator, wherein the humidification of the air is stopped by discharging stored water.
【請求項5】 請求項3記載の燃料電池発電装置におい
て、空気を加湿する加湿装置は、加湿用容器に貯留され
た水の中に空気を散気し、水中から脱気した空気を燃料
電池本体へ通流する構成を有し、前記空気の加湿停止
は、貯留された水を排出することにより行うように構成
したことを特徴とする固体高分子電解質型燃料電池発電
装置。
5. The fuel cell power generator according to claim 3, wherein the humidifier humidifies the air by diffusing the air into the water stored in the humidifying container and removing the air degassed from the water. A solid polymer electrolyte fuel cell power generator, characterized in that it has a configuration for flowing into a main body, and the humidification of the air is stopped by discharging stored water.
【請求項6】 請求項4または5に記載の燃料電池発電
装置において、加湿装置は、加湿膜主面の一側に貯留す
る水または加湿用容器に貯留される水を、別置の貯水タ
ンクからポンプ手段により導入・排出入するように構成
してなり、さらにこのポンプ手段は、少なくとも4つの
弁からなる流通方向切替手段を備え、前記制御装置は、
燃料電池発電装置の運転停止時に、前記流通方向切替に
より、貯留された水を排出するように構成したことを特
徴とする固体高分子電解質型燃料電池発電装置。
6. The fuel cell power generator according to claim 4, wherein the humidifying device separates water stored on one side of the humidifying film main surface or water stored in the humidifying container. And the pump means is configured to be introduced / discharged by a pump means. The pump means further includes a flow direction switching means including at least four valves, and the control device includes:
A solid polymer electrolyte fuel cell power generator, wherein the stored water is discharged by switching the flow direction when the operation of the fuel cell power generator is stopped.
【請求項7】 請求項4または5に記載の燃料電池発電
装置において、加湿装置は、さらに、無加湿空気を燃料
電池本体へ直接通流するバイパス回路とバイパス回路へ
の切替装置とを備え、前記空気の加湿停止は、空気の通
流をこのバイパス回路へ切り替えることにより行うよう
に構成したことを特徴とする固体高分子電解質型燃料電
池発電装置。
7. The fuel cell power generator according to claim 4, wherein the humidifier further comprises a bypass circuit for directly flowing non-humidified air to the fuel cell body, and a switching device for the bypass circuit. The solid polymer electrolyte fuel cell power generator is characterized in that the humidification of the air is stopped by switching the flow of air to the bypass circuit.
JP2000153001A 2000-05-24 2000-05-24 Solid polymer electrolyte fuel cell power generator and its operation method Expired - Fee Related JP4072707B2 (en)

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JP2003031254A (en) * 2001-07-16 2003-01-31 Fuji Electric Co Ltd Solid polymer electrolyte type fuel cell power generation device and its operating method
WO2003043113A1 (en) * 2001-11-13 2003-05-22 Nissan Motor Co., Ltd. Fuel cell system and method of stopping the system
JP2003203665A (en) * 2002-01-08 2003-07-18 Nissan Motor Co Ltd Fuel cell system
KR100444056B1 (en) * 2002-03-06 2004-08-11 현대자동차주식회사 Engine pre heating controlling device of fuel cell type vehicle and method thereof
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JP2004296384A (en) * 2003-03-28 2004-10-21 Osaka Gas Co Ltd Shutdown method of solid polymer type fuel cell and solid polymer type fuel cell
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JP2006086015A (en) * 2004-09-16 2006-03-30 Nissan Motor Co Ltd Fuel cell system
WO2006057134A1 (en) * 2004-11-29 2006-06-01 Nissan Motor Co., Ltd. Fuel cell system
US7157164B2 (en) 2002-04-19 2007-01-02 Toyota Jidosha Kabushiki Kaisha Fuel cell system and control method of the same
JP2007059129A (en) * 2005-08-23 2007-03-08 Nissan Motor Co Ltd Fuel cell system
WO2007063826A1 (en) * 2005-12-02 2007-06-07 Matsushita Electric Industrial Co., Ltd. Fuel cell system
WO2007066530A1 (en) * 2005-12-07 2007-06-14 Toyota Jidosha Kabushiki Kaisha Fuel battery system and mobile object
JP2007258020A (en) * 2006-03-23 2007-10-04 Osaka Gas Co Ltd Method of shutting down solid polymer fuel cell cogeneration system
KR101007153B1 (en) 2009-03-12 2011-01-12 한국에너지기술연구원 Optimized purge method for the durable fuel cell systems in below zero temperature condition
US7901826B2 (en) 2005-03-25 2011-03-08 Honda Motor Co., Ltd. Fuel cell
JP2011216498A (en) * 2011-08-01 2011-10-27 Nissan Motor Co Ltd Fuel cell system
US9425461B2 (en) * 2014-04-17 2016-08-23 Los Alamos National Security, Llc Rejuvenation of automotive fuel cells
WO2020177987A1 (en) * 2019-03-06 2020-09-10 Robert Bosch Gmbh Method for avoiding ice pressure damage in water-filled components of a fuel cell system

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62278766A (en) * 1986-05-28 1987-12-03 Fuji Electric Co Ltd Operating method for phosphoric acid fuel cell
JPH1167254A (en) * 1997-08-21 1999-03-09 Toshiba Corp Fuel cell power generating plant and its start/stop operation method
JP2000110727A (en) * 1998-10-07 2000-04-18 Toyota Autom Loom Works Ltd Antifreezing method for compressor for fuel cell system for vehicle
JP2001313055A (en) * 2000-04-28 2001-11-09 Equos Research Co Ltd Fuel cell device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62278766A (en) * 1986-05-28 1987-12-03 Fuji Electric Co Ltd Operating method for phosphoric acid fuel cell
JPH1167254A (en) * 1997-08-21 1999-03-09 Toshiba Corp Fuel cell power generating plant and its start/stop operation method
JP2000110727A (en) * 1998-10-07 2000-04-18 Toyota Autom Loom Works Ltd Antifreezing method for compressor for fuel cell system for vehicle
JP2001313055A (en) * 2000-04-28 2001-11-09 Equos Research Co Ltd Fuel cell device

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JP2003031254A (en) * 2001-07-16 2003-01-31 Fuji Electric Co Ltd Solid polymer electrolyte type fuel cell power generation device and its operating method
US6893758B2 (en) 2001-11-13 2005-05-17 Nissan Motor Co., Ltd. Fuel cell system and method of stopping the system
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