JP3416653B2 - Polymer electrolyte fuel cell power generator - Google Patents
Polymer electrolyte fuel cell power generatorInfo
- Publication number
- JP3416653B2 JP3416653B2 JP2001006349A JP2001006349A JP3416653B2 JP 3416653 B2 JP3416653 B2 JP 3416653B2 JP 2001006349 A JP2001006349 A JP 2001006349A JP 2001006349 A JP2001006349 A JP 2001006349A JP 3416653 B2 JP3416653 B2 JP 3416653B2
- Authority
- JP
- Japan
- Prior art keywords
- fuel cell
- water
- hot water
- temperature
- power generator
- 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.)
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Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Fuel Cell (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、例えば家庭用の小
型電源として好適な固体高分子形燃料電池発電装置に関
するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polymer electrolyte fuel cell power generator suitable as a small-sized power source for home use, for example.
【0002】[0002]
【従来の技術】近年、天然ガス、都市ガス、メタノー
ル、LPG、ブタンなどの燃料ガスを水素に改質する改
質器と、一酸化炭素を変成するCO変成器と、一酸化炭
素を除去するCO除去器と、起動時に各反応器が安定す
るまで水素を燃焼するプロセスガスバーナと、このよう
にして得られた水素と空気中の酸素とを化学反応させて
発電する燃料電池と、燃料電池の電極部を冷却するとと
もに反応空気の加湿のためのイオン交換樹脂などの水処
理装置で処理された水(純水)を収納した水タンクと、
前記改質器、燃料電池、プロセスガスバーナなどの排ガ
スの熱を回収して温水とする熱交換器と、この温水を蓄
える貯湯タンクなどを備えた小型電源としての固体高分
子形燃料電池発電装置が提案されている。2. Description of the Related Art Recently, a reformer for reforming a fuel gas such as natural gas, city gas, methanol, LPG, butane into hydrogen, a CO shifter for transforming carbon monoxide, and a carbon monoxide remover. A CO remover, a process gas burner that burns hydrogen until each reactor stabilizes at startup, a fuel cell that chemically reacts the hydrogen thus obtained with oxygen in the air, and a fuel cell A water tank containing water (pure water) treated with a water treatment device such as an ion exchange resin for cooling the electrode part and humidifying the reaction air,
A polymer electrolyte fuel cell power generator as a small power source equipped with a heat exchanger that recovers the heat of exhaust gas from the reformer, fuel cell, process gas burner and the like into hot water, and a hot water storage tank that stores the hot water. Proposed.
【0003】固体高分子形燃料電池発電装置で使用する
固体高分子電解質膜は含水させることによりプロトン導
電性電解質として機能するもので、固体高分子形燃料電
池においては、反応空気や燃料ガスなどの反応ガスに水
蒸気を飽和に含ませて電極部に供給して運転する方法が
採られている。A solid polymer electrolyte membrane used in a solid polymer fuel cell power generator functions as a proton conductive electrolyte by containing water. In the solid polymer fuel cell, reaction air, fuel gas, etc. A method is employed in which the reaction gas is saturated with water vapor and supplied to the electrode portion to operate.
【0004】燃料極に水素を含む燃料ガス、空気極に空
気を供給すると、燃料極では、水素分子を水素イオンと
電子に分解する燃料極反応、空気極では、酸素と水素イ
オンと電子から水を生成する以下の電気化学反応がそれ
ぞれ行われ、燃料極から空気極に向かって外部回路を移
動する電子により電力が負荷に供給されるとともに、空
気極側に水が生成される。When a fuel gas containing hydrogen is supplied to the fuel electrode and air is supplied to the air electrode, a fuel electrode reaction is carried out to decompose hydrogen molecules into hydrogen ions and electrons in the fuel electrode, and water is generated from oxygen, hydrogen ions and electrons in the air electrode. Each of the following electrochemical reactions that generate the electric current is performed, electric power is supplied to the load by the electrons moving in the external circuit from the fuel electrode toward the air electrode, and water is generated on the air electrode side.
【0005】図4は、従来の固体高分子形燃料電池発電
装置(PEFC装置GS)の系統図である。燃料電池6
を用いたPEFC装置GSは、例えば、燃料電池6の他
に熱回収,置RDを含んでいる。この熱回収装置RD
は、貯湯タンク50、熱交換器32、46、71、ポン
プ33、47、72とを備えた温水の循環路などで連結
されている。FIG. 4 is a system diagram of a conventional polymer electrolyte fuel cell power generator (PEFC device GS). Fuel cell 6
The PEFC apparatus GS using the above includes, for example, a heat recovery unit RD in addition to the fuel cell 6. This heat recovery device RD
Are connected by a hot water circulation path including a hot water storage tank 50, heat exchangers 32, 46, 71, and pumps 33, 47, 72.
【0006】燃料電池6は、脱硫器2、改質器3、CO
変成器4、CO除去器5などからなる燃料ガス供給装置
および空気ポンプ11、水タンク21などからなる反応
空気供給装置ならびに燃料極6a、空気極6kなどの電
極および水タンク21、ポンプ48、冷却部6cなどか
らなる燃料電池6の冷却装置を備えている。The fuel cell 6 comprises a desulfurizer 2, a reformer 3 and a CO
Fuel gas supply device including a transformer 4, CO remover 5 and the like, air pump 11, reaction air supply device including a water tank 21, electrodes such as fuel electrode 6a and air electrode 6k, and water tank 21, pump 48, cooling A cooling device for the fuel cell 6 including a portion 6c and the like is provided.
【0007】燃料電池6で発電された電力は図示しない
DC/DCコンバータで昇圧され、図示しない配電系統
連携インバータを介して商用電源に接続される、一方、
ここから家庭や事務所などの照明や空調機のの他の電気
機器用の電力として供給される。The electric power generated by the fuel cell 6 is boosted by a DC / DC converter (not shown) and connected to a commercial power source through an unillustrated power distribution system cooperation inverter.
Electric power is supplied from here to other electric appliances such as lighting and air conditioners in homes and offices.
【0008】このような燃料電池6を用いたPEFC装
置GSでは、発電と同時に、例えば燃料電池6による発
電時に発生する熱を利用して市水から温水を生成し、こ
の温水を貯湯タンク50に蓄えて、風呂や台所などに供
給するなど、燃料電池6に使用される燃料がもつエネル
ギーの有効利用を図っている。In the PEFC device GS using such a fuel cell 6, hot water is generated from city water by utilizing heat generated during power generation by the fuel cell 6 simultaneously with power generation, and the hot water is stored in the hot water storage tank 50. The energy stored in the fuel used in the fuel cell 6 is effectively used by storing it and supplying it to a bath or kitchen.
【0009】上記のPEFC装置GSの燃料ガス供給装
置では、天然ガス、都市ガス、メタノール、LPG、ブ
タンなどの原燃料1が脱硫器2に供給され、ここで原燃
料から硫黄成分が除去される。この脱硫器2を経た原燃
料は、昇圧ポンプ10で昇圧されて改質器3に供給され
る際に、水タンク21から水ポンプ22を経て温水が送
られ、熱交換器17で加熱されて生成した水蒸気と合流
して、供給される。改質器3では、水素、二酸化炭素、
および一酸化炭素を含む改質ガスが生成される。この改
質器3を経たガスは、CO変成器4に供給され、ここで
は改質ガスに含まれる一酸化炭素が二酸化炭素に変成さ
れる。このCO変成器4を経たガスは、CO除去器5に
供給され、ここではCO変成器4を経たガス中の未変成
の一酸化炭素が例えば10ppm以下に低減され、水素
濃度の高い水性ガス(改質ガス)がパイプ64を経て燃
料電池6の燃料極6aに供給される。In the fuel gas supply device of the PEFC device GS described above, the raw fuel 1 such as natural gas, city gas, methanol, LPG, butane is supplied to the desulfurizer 2, where the sulfur component is removed from the raw fuel. . When the raw fuel that has passed through the desulfurizer 2 is pressurized by the booster pump 10 and supplied to the reformer 3, hot water is sent from the water tank 21 through the water pump 22 and heated by the heat exchanger 17. It is supplied together with the generated steam. In the reformer 3, hydrogen, carbon dioxide,
A reformed gas containing carbon monoxide and carbon monoxide is produced. The gas that has passed through the reformer 3 is supplied to the CO shift converter 4, where carbon monoxide contained in the reformed gas is transformed into carbon dioxide. The gas that has passed through the CO shift converter 4 is supplied to the CO remover 5, where the untransformed carbon monoxide in the gas that has passed through the CO shift converter 4 is reduced to, for example, 10 ppm or less, and the water gas having a high hydrogen concentration ( The reformed gas) is supplied to the fuel electrode 6a of the fuel cell 6 through the pipe 64.
【0010】このとき、水タンク21から改質器3へ供
給される温水の量を調節することにより改質ガスへの水
分の添加量が調節される。反応空気供給装置では、空気
ポンプ11から水タンク21に、空気を供給し、水タン
ク21内の温水中に反応空気を泡立てつつ気相部53に
送出することによって加湿が行われる。このようにし
て、燃料電池6における反応が適度に維持されるように
水分を与えられた後の反応空気が水タンク21からパイ
プ25を経て燃料電池6の空気極6kに供給される。At this time, the amount of water added to the reformed gas is adjusted by adjusting the amount of hot water supplied from the water tank 21 to the reformer 3. In the reaction air supply device, humidification is performed by supplying air from the air pump 11 to the water tank 21 and bubbling the reaction air into the hot water in the water tank 21 and sending the reaction air to the gas phase portion 53. In this way, the reaction air that has been moistened so that the reaction in the fuel cell 6 is appropriately maintained is supplied from the water tank 21 through the pipe 25 to the air electrode 6k of the fuel cell 6.
【0011】燃料電池6では、燃料極6aに供給された
改質ガス中の水素と、空気ポンプ11、水タンク21の
気相部53を経て空気極6kへ供給された空気中の酸素
との電気化学反応によって発電が行われる。燃料電池6
の冷却装置は、この電気化学反応の反応熱などで燃料電
池6が過熱しないようにするため、燃料電池6の電極6
a、6kに並置された冷却装置であり、冷却部6cに水
タンク21の温水をポンプ48で冷却水として循環さ
せ、この冷却水で燃料電池6内の温度が発電に適した温
度(例えば70〜80℃程度)に保たれるように制御し
ている。In the fuel cell 6, the hydrogen in the reformed gas supplied to the fuel electrode 6a and the oxygen in the air supplied to the air electrode 6k via the air pump 11 and the gas phase portion 53 of the water tank 21 are used. Power is generated by an electrochemical reaction. Fuel cell 6
In order to prevent the fuel cell 6 from overheating due to the reaction heat of this electrochemical reaction, the cooling device of FIG.
a, 6k are juxtaposed with each other. Hot water in the water tank 21 is circulated as cooling water by the pump 48 in the cooling unit 6c, and the temperature in the fuel cell 6 is suitable for power generation (for example, 70 The temperature is controlled to be maintained at about 80 ° C.
【0012】改質器3における化学反応は吸熱反応であ
るので、加熱しながら化学反応を継続させるためのバー
ナ12を有し、ここにはパイプ13を介して原燃料が供
給され、ファン14を介して空気が供給され、パイプ1
5を介して、燃料極6aを経た未反応水素が供給され
る。本PEFC装置GSの始動時には、バーナ12にパ
イプ13を介して原燃料が供給されて燃焼が行われ、起
動後に、燃料電池6の温度が安定したときにはに、パイ
プ13からの原燃料の供給が断たれ、替わりにパイプ1
5を介して燃料極6aから排出される未反応水素(オフ
ガス)が供給されて燃焼が継続される。Since the chemical reaction in the reformer 3 is an endothermic reaction, it has a burner 12 for continuing the chemical reaction while heating, to which raw fuel is supplied via a pipe 13 and a fan 14 is connected. Air is supplied through the pipe 1
Unreacted hydrogen that has passed through the fuel electrode 6 a is supplied via 5. At the time of starting the PEFC device GS, the raw fuel is supplied to the burner 12 via the pipe 13 to perform combustion, and when the temperature of the fuel cell 6 becomes stable after the start, the supply of the raw fuel from the pipe 13 is performed. Broken, pipe 1 instead
Unreacted hydrogen (off gas) discharged from the fuel electrode 6a is supplied via 5 to continue combustion.
【0013】一方、CO変成器4、CO除去器5で行わ
れる化学反応は発熱反応である。運転中は、発熱反応の
熱により反応温度以上に昇温しないように冷却制御が行
われる。このようにして改質器3、CO変成器4、CO
除去器5および燃料電池6では所定の化学反応と発電が
継続される。On the other hand, the chemical reaction carried out in the CO shift converter 4 and the CO remover 5 is an exothermic reaction. During operation, cooling control is performed so that the heat of the exothermic reaction does not raise the temperature above the reaction temperature. In this way, the reformer 3, the CO converter 4, the CO
A predetermined chemical reaction and power generation are continued in the remover 5 and the fuel cell 6.
【0014】上記改質器3とCO変成器4間、CO変成
器4とCO除去器5間にはそれぞれ熱交換器18、19
が接続されている。そして各熱交換器18、19には水
タンク21の温水が、ポンプ23、24を介して循環
し、これらの温水で改質器3、CO変成器4を経たガス
がそれぞれ冷却される。図示しないがCO除去器5と燃
料電池6との間にも熱交換器を接続してCO除去器5を
経たガスを冷却することができる。上記改質器3の排気
系31には熱交換器17が接続され、水タンク21の温
水がポンプ22を介して供給されると、この熱交換器1
7で水蒸気化し、この水蒸気が原燃料と混合して改質器
3に供給される。Heat exchangers 18 and 19 are provided between the reformer 3 and the CO shift converter 4 and between the CO shift converter 4 and the CO remover 5, respectively.
Are connected. The hot water in the water tank 21 circulates through the heat exchangers 18 and 19 via the pumps 23 and 24, and the hot water cools the gas passing through the reformer 3 and the CO shift converter 4, respectively. Although not shown, a heat exchanger may be connected between the CO remover 5 and the fuel cell 6 to cool the gas passing through the CO remover 5. The heat exchanger 17 is connected to the exhaust system 31 of the reformer 3, and when the hot water in the water tank 21 is supplied via the pump 22, the heat exchanger 1
It is vaporized at 7, and this vapor is mixed with the raw fuel and supplied to the reformer 3.
【0015】PEFC装置GSには、プロセスガスバー
ナ(PGバーナ)34が備えられている。PEFC装置
GSの起動時には、改質器3、CO変成器4、CO除去
器5を経た改質ガスの組成が燃料電池6の運転に適した
安定した規定値に達していないので、それが安定するま
では、このガスを燃料電池6に供給することができな
い。そこで、各反応器が安定するまでは、ガス組成が規
定値に達していないガスをこのPGバーナ34に導いて
燃焼させる。37はPGバーナ34に燃焼用空気を送る
ファンである。The PEFC device GS is provided with a process gas burner (PG burner) 34. At the time of starting the PEFC device GS, the composition of the reformed gas that has passed through the reformer 3, the CO shifter 4, and the CO remover 5 has not reached a stable specified value suitable for the operation of the fuel cell 6, so that it is stable. Until then, this gas cannot be supplied to the fuel cell 6. Therefore, until the respective reactors become stable, the gas whose gas composition has not reached the specified value is introduced into the PG burner 34 and burned. Reference numeral 37 is a fan that sends combustion air to the PG burner 34.
【0016】そして、各反応器が安定しガス中のCO濃
度が規定値(例えば、10〜20ppm以下)に達した
後、燃料電池6に導入して発電を行う。燃料電池6での
発電に使用できなかった未反応ガスは、当初PGバーナ
34に導いて燃焼し、燃料電池6の温度が安定した後
は、燃料電池6からのオフガスをパイプ15経由、改質
器3のバーナ12に導入して燃焼させる。Then, after each reactor is stabilized and the CO concentration in the gas reaches a specified value (for example, 10 to 20 ppm or less), it is introduced into the fuel cell 6 to generate electricity. The unreacted gas that could not be used for power generation in the fuel cell 6 was initially guided to the PG burner 34 and burned, and after the temperature of the fuel cell 6 became stable, the off gas from the fuel cell 6 was reformed through the pipe 15 and reformed. It is introduced into the burner 12 of the vessel 3 and burned.
【0017】すなわち、PEFC装置GSの起動後、各
反応器が温度的に安定するまでは、開閉弁91が閉じら
れ、改質ガスは管路35および開閉弁36を経てPGバ
ーナ34に供給される。That is, after the PEFC unit GS is started, the on-off valve 91 is closed and the reformed gas is supplied to the PG burner 34 via the pipe line 35 and the on-off valve 36 until the temperature of each reactor becomes stable. It
【0018】各反応器が温度的に安定した場合、今度は
燃料電池6の温度が作動温度(例えば70〜80℃)近
くの温度域で安定するまで、開閉弁91が開かれ、開閉
弁92が閉じられて、改質ガスが管路38および開閉弁
39を経てPGバーナ34に供給され、そこで燃焼され
る。When the temperature of each reactor is stable, the on-off valve 91 is opened and the on-off valve 92 is opened until the temperature of the fuel cell 6 stabilizes in the temperature range near the operating temperature (for example, 70 to 80 ° C.). Is closed, and the reformed gas is supplied to the PG burner 34 via the pipe 38 and the opening / closing valve 39, and is burned there.
【0019】燃料電池6の温度が作動温度で安定し、連
続して発電が行われるようになった場合、開閉弁91、
開閉弁92が開かれ、開閉弁36、開閉弁39が閉じら
れて、燃料電池6を経た未反応ガス(オフガス)は管路
15を経てバーナ12に供給される。When the temperature of the fuel cell 6 is stabilized at the operating temperature and power is continuously generated, the on-off valve 91,
The on-off valve 92 is opened, the on-off valve 36 and the on-off valve 39 are closed, and the unreacted gas (off gas) that has passed through the fuel cell 6 is supplied to the burner 12 via the pipe 15.
【0020】貯湯タンク50には水道管61を経て市水
が供給される。この貯湯タンク50に供給された市水
は、PEFC装置GSから発生する排熱によって加熱さ
れ、この昇温された温水は、温水供給管62を通じて外
部に給湯される。例えば排気系31には、熱交換器17
の他に、さらに別の熱交換器32が接続され、この熱交
換器32には貯湯タンク50の水が、ポンプ33を介し
て循環し、排熱回収が行われる。City water is supplied to the hot water storage tank 50 through a water pipe 61. The city water supplied to the hot water storage tank 50 is heated by the exhaust heat generated from the PEFC device GS, and the heated hot water is supplied to the outside through the hot water supply pipe 62. For example, the exhaust system 31 includes a heat exchanger 17
In addition to the above, another heat exchanger 32 is connected, and the water in the hot water storage tank 50 circulates in the heat exchanger 32 via the pump 33 to recover the exhaust heat.
【0021】またPGバーナ34の排気系45には、熱
交換器46が接続され、この熱交換器46には、ポンプ
47を介して貯湯タンク50の水が循環され貯湯タンク
50に熱回収が行われる。水タンク21には、ポンプ2
3、24、48によって熱交換器18、19を経て戻る
水や燃料電池6の冷却部6cを循環する冷却水が水管7
3を経て流入する一方、水タンク21に水を供給する水
補給装置68が接続されている。水補給装置68は電動
弁56と供給タンク67およびポンプ74などから構成
されている。供給タンク67は市水補給装置69および
燃料電池6から生じる水をパイプ70を経て一旦貯えて
水タンク21に水を供給できるようにしたタンクであ
る。A heat exchanger 46 is connected to the exhaust system 45 of the PG burner 34, and water in the hot water storage tank 50 is circulated through the heat exchanger 46 via a pump 47 to recover heat in the hot water storage tank 50. Done. The water tank 21 has a pump 2
The water returning through the heat exchangers 18 and 19 by the cooling devices 3, 24 and 48 and the cooling water circulating in the cooling portion 6c of the fuel cell 6 are the water pipes 7.
A water supply device 68 is connected to supply water to the water tank 21 while flowing in through The water replenishing device 68 is composed of an electric valve 56, a supply tank 67, a pump 74, and the like. The supply tank 67 is a tank capable of temporarily storing water generated from the city water supply device 69 and the fuel cell 6 via the pipe 70 and supplying the water to the water tank 21.
【0022】燃料電池6から生じる水には、例えば、燃
料電池6の空気極6kから排出されたガスを熱交換器7
1に導き、この熱交換器71中をポンプ72によって貯
湯タンク50との間を循環する水で冷却することによっ
て得られたドレン水や燃料極6aから排出されたガスに
含まれている水がある。For the water generated from the fuel cell 6, for example, the gas discharged from the air electrode 6k of the fuel cell 6 is used as the heat exchanger 7.
1 and the drain water obtained by cooling the inside of the heat exchanger 71 with the water circulating between the heat exchanger 71 and the hot water storage tank 50 and the water contained in the gas discharged from the fuel electrode 6a. is there.
【0023】市水補給装置69は、電動弁76を有する
水道管52を介して水源78に接続されており、供給タ
ンク67の水量が減って水位が低下したことを水位計7
9が検知したときに液面制御装置77が電動弁76を開
き、水源78の水圧を利用して水道管52、水処理装置
(イオン交換樹脂)51を経て供給タンク67に水を補
給し、水タンク21に水を供給するのに支障のない水量
を保持する装置である。水タンク21には、タンク内の
上部に常に空気部分(気相部)53が形成されるように
水の水位を保つ液面制御装置LCおよび水タンク21内
の水温を設定範囲に保つ温度調節装置TCとを有してい
る。The city water supply device 69 is connected to the water source 78 through the water pipe 52 having the motor-operated valve 76, and indicates that the water level in the supply tank 67 has decreased and the water level has decreased.
When 9 detects, the liquid level control device 77 opens the motor-operated valve 76 and utilizes the water pressure of the water source 78 to supply water to the supply tank 67 via the water pipe 52 and the water treatment device (ion exchange resin) 51. It is a device that holds the amount of water that does not hinder the supply of water to the water tank 21. In the water tank 21, a liquid level control device LC that keeps the water level of water so that an air portion (vapor phase portion) 53 is always formed in the upper part of the tank, and temperature control that keeps the water temperature in the water tank 21 within a set range. And a device TC.
【0024】液面制御装置LCは、水位計54と電動弁
56の制御装置を備えて水タンク21内の水量を常時監
視しつつ、反応用空気が、水タンク21の中を通過する
際に適度に加湿されて燃料電池6に供給されるようにタ
ンク内に水を貯え、かつ上部に気相部53が形成される
ように水量を制御し、水位が低下した場合はポンプ74
を運転し、電動弁56の開度を調節して供給タンク67
からパイプ84を経て処理水を導入し、水タンク21内
の水位を設定範囲に保つようにしている。55は、水位
計54による水位の検出が泡立ちなどにより不安定にな
るのを防止する消波板である。The liquid level control device LC is provided with a control device for the water level gauge 54 and the motor-operated valve 56 to constantly monitor the amount of water in the water tank 21, and when the reaction air passes through the water tank 21. Water is stored in the tank so as to be appropriately humidified and supplied to the fuel cell 6, and the amount of water is controlled so that the gas phase portion 53 is formed in the upper part. When the water level drops, the pump 74
Of the supply tank 67 by adjusting the opening degree of the motor-operated valve 56.
The treated water is introduced from the above through the pipe 84 to keep the water level in the water tank 21 within the set range. Reference numeral 55 is a wave-eliminating plate that prevents the detection of the water level by the water level gauge 54 from becoming unstable due to foaming or the like.
【0025】温度調節装置TCは、燃料電池6の空気極
6kに反応空気を供給する際に、水タンク21内で適度
に加湿が行えるように水の温度を例えば60〜80℃の
温度範囲(設定温度)に保つ装置である。63はバブリ
ング用の多孔板である。The temperature control device TC controls the temperature of the water in a temperature range of, for example, 60 to 80 ° C. so that the water can be appropriately humidified when the reaction air is supplied to the air electrode 6k of the fuel cell 6. It is a device that keeps the temperature at the set temperature. 63 is a perforated plate for bubbling.
【0026】[0026]
【発明が解決しようとする課題】以上のような構成のP
EFC装置GSは、発電と熱利用のコジェネレーション
システムの形態をとるので、燃料電池の発電効率が図ら
れるばかりでなく、このシステムで使用される水の有効
な再利用が図られる効果がある。しかし、装置停止時
に、例えば水タンク21内の水の温度が低下して凍結す
ると、水タンク21や燃料電池6が損傷を受けるととも
に、水系統の配管、弁、ポンプなどが損傷を受け、装置
を再起動できなくなる重大な問題が発生する。[Problems to be Solved by the Invention]
Since the EFC device GS takes the form of a cogeneration system for power generation and heat utilization, not only the power generation efficiency of the fuel cell is achieved, but also the effective reuse of the water used in this system is achieved. However, if the temperature of the water in the water tank 21 drops and freezes when the device is stopped, the water tank 21 and the fuel cell 6 will be damaged, and the piping, valves, pumps, etc. of the water system will be damaged, and the device will be damaged. There is a serious problem that prevents you from restarting.
【0027】本発明の目的は、従来の上記問題を解決
し、装置停止時における水系統の凍結を防止して、凍結
による水タンク21、燃料電池6、貯湯タンク50、水
系統の熱交換器32、46、71など、配管類、弁類、
ポンプ類、パイプ類などが損傷を受けるのを防止した信
頼性の高い、例えば家庭用などに使用できる小型電源と
して好適な固体高分子形燃料電池発電装置を提供するこ
とである。The object of the present invention is to solve the above-mentioned problems of the prior art and prevent freezing of the water system when the apparatus is stopped, and to prevent the water tank 21, the fuel cell 6, the hot water storage tank 50, and the heat exchanger of the water system from freezing. 32, 46, 71, etc., piping, valves,
It is an object of the present invention to provide a highly reliable polymer electrolyte fuel cell power generator which is highly reliable and is suitable as a small-sized power source that can be used for household purposes, for example, which prevents damage to pumps, pipes and the like.
【0028】[0028]
【課題を解決するための手段】すなわち、本発明の請求
項1の固体高分子形燃料電池発電装置は、天然ガス、都
市ガス、メタノール、LPG、ブタンなどの燃料ガスを
水素に改質する改質器と、一酸化炭素を変成するCO変
成器と、一酸化炭素を除去するCO除去器と、起動時に
各反応器が安定するまで水素を燃焼するプロセスガスバ
ーナと、水素によって発電する燃料電池と、燃料電池を
冷却するための水を収納した水タンクと、前記改質器、
燃料電池、プロセスガスバーナなどの排ガスの熱を回収
して温水とする熱交換器と、この温水を蓄える貯湯タン
クとを備えた固体高分子形燃料電池発電装置であって、
装置停止時に水系統が凍結する恐れがある場合は、それ
を検知して前記プロセスガスバーナを燃焼させて前記貯
湯タンクの温水を昇温し前記水系統の一部あるいは全部
に循環して送って凍結防止する制御システムを備えたこ
とを特徴とするものである。That is, the polymer electrolyte fuel cell power generator according to claim 1 of the present invention is a reformer for reforming fuel gas such as natural gas, city gas, methanol, LPG, butane into hydrogen. A gas purifier, a CO shifter that transforms carbon monoxide, a CO remover that removes carbon monoxide, a process gas burner that burns hydrogen until each reactor stabilizes at startup, and a fuel cell that generates electricity by hydrogen A water tank containing water for cooling the fuel cell, the reformer,
A polymer electrolyte fuel cell power generator comprising a heat exchanger that recovers heat of exhaust gas such as a fuel cell and a process gas burner into hot water, and a hot water storage tank that stores the hot water,
If there is a risk that the water system will freeze when the equipment is stopped, it is detected and the process gas burner is burned to raise the temperature of the hot water in the hot water storage tank and circulate it to part or all of the water system to freeze it. It is characterized by having a control system for preventing it.
【0029】また、本発明の請求項2の固体高分子形燃
料電池発電装置は、天然ガス、都市ガス、メタノール、
LPG、ブタンなどの燃料ガスを水素に改質する改質器
と、一酸化炭素を変成するCO変成器と、一酸化炭素を
除去するCO除去器と、起動時に各反応器が安定するま
で水素を燃焼するプロセスガスバーナと、水素によって
発電する燃料電池と、燃料電池を冷却するための水を収
納した水タンクと、前記改質器、燃料電池、プロセスガ
スバーナなどの排ガスの熱を回収して温水とする熱交換
器と、この温水を蓄える貯湯タンクとを備えた固体高分
子形燃料電池発電装置であって、装置停止時に水系統が
凍結する恐れがある場合は、それを検知して前記プロセ
スガスバーナを燃焼させずに前記貯湯タンクの温水を前
記水系統の一部あるいは全部に循環して送って凍結防止
する制御システムを備えたことを特徴とする。The polymer electrolyte fuel cell power generator according to claim 2 of the present invention comprises natural gas, city gas, methanol,
A reformer that reforms fuel gas such as LPG and butane to hydrogen, a CO shifter that transforms carbon monoxide, a CO remover that removes carbon monoxide, and hydrogen until each reactor stabilizes at startup. Process gas burner that burns, a fuel cell that generates electricity by hydrogen, a water tank that stores water for cooling the fuel cell, and heat of exhaust gas from the reformer, fuel cell, process gas burner, etc. A solid polymer electrolyte fuel cell power generator comprising a heat exchanger for storing the hot water and a hot water storage tank for storing the hot water, and when the water system may freeze when the device is stopped, the process is detected by detecting it. A control system is provided, which circulates and sends hot water in the hot water storage tank to part or all of the water system without burning the gas burner to prevent freezing.
【0030】本発明の請求項3の固体高分子形燃料電池
発電装置は、請求項1あるいは請求項2記載の固体高分
子形燃料電池発電装置において、燃料電池の冷却部に冷
却水を送るポンプを作動させ、前記水タンク内の水を循
環して燃料電池本体を暖めて凍結を防止することを特徴
とする。A polymer electrolyte fuel cell power generator according to claim 3 of the present invention is the polymer electrolyte fuel cell power generator according to claim 1 or 2, wherein a pump for sending cooling water to the cooling portion of the fuel cell. Is operated to circulate the water in the water tank to warm the fuel cell body to prevent freezing.
【0031】本発明の請求項4の固体高分子形燃料電池
発電装置は、請求項1から請求項3のいずれかに記載の
固体高分子形燃料電池発電装置において、前記水タンク
あるいは燃料電池本体の温度がある定められた温度以上
になると、前記プロセスガスバーナの燃焼を行っている
場合はそれを停止し、かつ排熱回収用ポンプを停止する
ことを特徴とする。The polymer electrolyte fuel cell power generator according to claim 4 of the present invention is the polymer electrolyte fuel cell power generator according to any one of claims 1 to 3, wherein the water tank or the fuel cell main body is used. When the temperature exceeds a predetermined temperature, the process gas burner is stopped if it is burning, and the exhaust heat recovery pump is stopped.
【0032】本発明の請求項5の固体高分子形燃料電池
発電装置は、請求項1、請求項3あるいは請求項4記載
の固体高分子形燃料電池発電装置において、凍結を検知
する手段が前記水タンクの温度を検知する手段であり、
水タンクの温度がある定められた値以下になった場合
に、前記プロセスガスバーナを燃焼させて前記貯湯タン
クの温水を昇温し前記水系統の一部あるいは全部に循環
して送って凍結防止することを特徴とする。The polymer electrolyte fuel cell power generator according to claim 5 of the present invention is the polymer electrolyte fuel cell power generator according to claim 1, claim 3 or claim 4, wherein the means for detecting freezing is the Is a means to detect the temperature of the water tank,
When the temperature of the water tank falls below a predetermined value, the process gas burner is burned to raise the hot water in the hot water storage tank and is circulated to part or all of the water system to be sent to prevent freezing. It is characterized by
【0033】本発明の請求項6の固体高分子形燃料電池
発電装置は、請求項1、請求項3、請求項4あるいは請
求項5記載の固体高分子形燃料電池発電装置において、
凍結を検知する手段が燃料電本体の温度を検知する手段
であり、燃料電池本体の温度がある定められた値以下に
なった場合に、前記プロセスガスバーナを燃焼させて前
記貯湯タンクの温水を昇温し前記水系統の一部あるいは
全部に循環して送って凍結防止することを特徴とする。According to a sixth aspect of the present invention, there is provided a polymer electrolyte fuel cell power generator according to any one of the first, third, fourth and fifth polymer electrolyte fuel cell power generators.
The means for detecting freezing is a means for detecting the temperature of the fuel cell main body, and when the temperature of the fuel cell main body falls below a predetermined value, the process gas burner is burned to raise the hot water in the hot water storage tank. It is characterized in that it is heated and circulated to a part or the whole of the water system to prevent freezing.
【0034】本発明の請求項7の固体高分子形燃料電池
発電装置は、請求項1、請求項3、請求項4、請求項5
あるいは請求項6記載の固体高分子形燃料電池発電装置
において、凍結を検知する手段が固体高分子形燃料電池
発電装置内の雰囲気の温度を検知する手段であり、前記
雰囲気の温度がある定められた値以下になった場合に、
前記プロセスガスバーナを燃焼させて前記貯湯タンクの
温水を昇温し前記水系統の一部あるいは全部に循環して
送って凍結防止することを特徴とする。According to a seventh aspect of the present invention, there is provided a polymer electrolyte fuel cell power generation device according to the first aspect, the third aspect, the fourth aspect, the fifth aspect.
Alternatively, in the polymer electrolyte fuel cell power generator according to claim 6, the means for detecting freezing is a means for detecting the temperature of the atmosphere in the polymer electrolyte fuel cell power generator, and the temperature of the atmosphere is determined. When the value is less than
It is characterized in that the process gas burner is burned to raise the temperature of the hot water in the hot water storage tank, and the hot water is circulated and sent to part or all of the water system to prevent freezing.
【0035】本発明の固体高分子形燃料電池発電装置
は、装置停止時に、例えば水タンク21内の水の温度が
低下して約2℃以下になると、あるいは燃料電池6本体
の温度や固体高分子形燃料電池発電装置内の雰囲気の温
度が低下して凍結する恐れがある場合は、それらを検知
して前記プロセスガスバーナ34を燃焼させて前記貯湯
タンク50の温水を昇温し水タンク21を含む前記水系
統の一部あるいは全部に循環して送るとともにポンプ4
8を作動させて燃料電池6の冷却部6cに温水を循環し
て送って燃料電池6本体の温度を上昇させて凍結防止し
たり、あるいはプロセスガスバーナ34を燃焼させずに
貯湯タンク50の温水を前記水系統の一部あるいは全部
に循環して送って凍結防止する制御システムを備えたの
で、凍結による燃料電池6本体、水タンク21、燃料電
池6、貯湯タンク50、水系統の熱交換器32、46、
71など、配管類、弁類、ポンプ類、パイプ類などが損
傷を受けるのを防止でき、寒冷地や冬季における保守作
業を省力化できるとともに、信頼性が向上し、例えば、
寒冷地における家庭用小型電源などに好ましく使用でき
る。In the polymer electrolyte fuel cell power generator of the present invention, for example, when the temperature of the water in the water tank 21 decreases to about 2 ° C. or less when the apparatus is stopped, or the temperature of the fuel cell 6 or the solid height increases. When the temperature of the atmosphere in the molecular fuel cell power generator is lowered and there is a risk of freezing, these are detected and the process gas burner 34 is burned to raise the temperature of the hot water in the hot water storage tank 50 and the water tank 21. Including and circulating the water to part or all of the water system including the pump 4
8 is operated to circulate and send hot water to the cooling part 6c of the fuel cell 6 to raise the temperature of the fuel cell 6 main body to prevent freezing, or to heat the hot water of the hot water storage tank 50 without burning the process gas burner 34. Since a control system for circulating and sending to part or all of the water system to prevent freezing is provided, the fuel cell 6 main body, the water tank 21, the fuel cell 6, the hot water tank 50, and the heat exchanger 32 of the water system due to freezing are provided. , 46,
71, etc., pipes, valves, pumps, pipes, etc. can be prevented from being damaged, maintenance work in cold regions and winter can be labor-saving, and reliability is improved.
It can be preferably used for household small power sources in cold regions.
【0036】[0036]
【発明の実施の形態】以下、本発明の実施の形態を図面
を用いて詳細に説明する。図1〜3は、本発明の固体高
分子形燃料電池発電装置の実施形態を説明する系統図で
ある。図1〜3において、図4に示した構成部分と同じ
構成部分には同一参照符号を付すことにより、重複した
説明を省略する。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below with reference to the drawings. 1 to 3 are system diagrams for explaining an embodiment of a polymer electrolyte fuel cell power generator of the present invention. 1 to 3, the same components as those shown in FIG. 4 are designated by the same reference numerals, and the duplicated description will be omitted.
【0037】図1に示した本発明の固体高分子形燃料電
池発電装置GS1は、排気系31の熱交換器32、排気
系45の熱交換器46および燃料電池6の空気極kから
排出されたガスの熱交換器71の後に、さらに熱交換器
HEXを設置し、貯湯タンク50中の水をポンプPによ
りこの熱交換器HEXを経て、熱交換器71、32、4
6に送って熱交換して排熱回収した温水Aを、直接水タ
ンク21へ熱交換可能に循環して送るラインL1を設け
てある。そして、前記温水AをラインL1を経て水タン
ク21へ送らなくてもよい場合に温水Aを貯湯タンク5
0へ送るラインL2が併設されており、ラインL1には
開閉弁82、ラインL2には開閉弁81がそれぞれ設け
てある。T1はパイプ(水管)73に設けられた温度計
で燃料電池6の冷却部6cを循環する冷却水の温度を検
知する手段であり、T2は水タンク21中に設けられた
温度計であり水タンク21の温度を検知する手段であ
る。また図示しないが燃料電池6には燃料電池6本体の
温度を検知する手段(温度計)が取り付けられており、
さらに図示しないが固体高分子形燃料電池発電装置GS
1には装置内部の雰囲気の温度を検知する手段(温度
計)が取り付けられている。本発明の固体高分子形燃料
電池発電装置GS1はこのような熱回収装置RD1など
を備えた以外は図4に示した固体高分子形燃料電池発電
装置GSと同様になっている。The polymer electrolyte fuel cell power generator GS1 of the present invention shown in FIG. 1 is discharged from the heat exchanger 32 of the exhaust system 31, the heat exchanger 46 of the exhaust system 45 and the air electrode k of the fuel cell 6. After the heat exchanger 71 for the gas, a heat exchanger HEX is further installed, and the water in the hot water storage tank 50 is pumped through the heat exchanger HEX by the pump P to the heat exchangers 71, 32, 4
A line L1 is provided to circulate and send the hot water A, which is sent to 6 to perform heat exchange and recovers waste heat, directly to the water tank 21 so as to be heat-exchanged. When the hot water A does not have to be sent to the water tank 21 via the line L1, the hot water A is stored in the hot water storage tank 5
A line L2 for sending to 0 is provided side by side, an opening / closing valve 82 is provided in the line L1, and an opening / closing valve 81 is provided in the line L2. T1 is a thermometer provided in the pipe (water pipe) 73 for detecting the temperature of the cooling water circulating in the cooling section 6c of the fuel cell 6, and T2 is a thermometer provided in the water tank 21 for It is a means for detecting the temperature of the tank 21. Although not shown, the fuel cell 6 is provided with means (thermometer) for detecting the temperature of the fuel cell 6 main body,
Further, although not shown, a polymer electrolyte fuel cell power generator GS
1 is equipped with means (thermometer) for detecting the temperature of the atmosphere inside the apparatus. The polymer electrolyte fuel cell power generator GS1 of the present invention is the same as the polymer electrolyte fuel cell generator GS shown in FIG. 4 except that such a heat recovery device RD1 is provided.
【0038】(本発明の固体高分子形燃料電池発電装置
GS1の停止時、水タンク21中の水が凍結する恐れが
ある場合)水タンク21の水温(温度計T2で常時監視
して測定される水温)が設定温度以下(例えば2℃以
下)になって凍結する恐れがある場合、図示しない制御
装置から信号をPGバーナ34、ファン37、開閉弁8
1、82、ポンプPに送って、ファン37を作動させ、
PGバーナ34を作動させて点火するとともに、ライン
L2の開閉弁81を閉め、ラインL1の開閉弁82を開
け、そしてポンプPを作動させて、PGバーナ34に連
結された熱交換器46で熱回収され昇温した温水Aを含
む貯湯タンク50の温水をラインL1に循環して送っ
て、水タンク21中の水を加熱する(図2参照。太実線
で温水の流れを示す。開閉弁81、82の開閉状態、フ
ァン37およびPGバーナ34の作動状況を図2中の表
に示す)。(When the polymer electrolyte fuel cell power generator GS1 of the present invention is stopped, the water in the water tank 21 may freeze) The water temperature of the water tank 21 (measured by a thermometer T2 at all times for monitoring). When there is a risk that the temperature of the water to be cooled becomes equal to or lower than the set temperature (for example, 2 ° C. or lower), the control device (not shown) sends a signal to the PG burner 34, the fan 37, and the open / close valve 8.
1, 82, send to the pump P, to operate the fan 37,
The PG burner 34 is operated to ignite, the opening / closing valve 81 of the line L2 is closed, the opening / closing valve 82 of the line L1 is opened, and the pump P is operated to generate heat by the heat exchanger 46 connected to the PG burner 34. The hot water in the hot water storage tank 50 containing the recovered and heated hot water A is circulated and sent to the line L1 to heat the water in the water tank 21 (see FIG. 2. The thick solid line indicates the flow of the hot water. Open / close valve 81 , 82, the operating states of the fan 37 and the PG burner 34 are shown in the table in FIG.
【0039】さらに燃料電池6本体の温度を検知する図
示しない手段(温度計)が設定温度以下(例えば2℃以
下)になって燃料電池6本体が凍結する恐れがある場
合、同様にしてPGバーナ34を作動させて上記のよう
に温水を循環するとともに図示しない制御装置から信号
をポンプ48に送ってポンプ48を作動させて燃料電池
6の冷却部6cに温水を循環して送って燃料電池6本体
の温度を上昇させて凍結防止する。Further, when a means (thermometer) (not shown) for detecting the temperature of the fuel cell 6 body becomes lower than a set temperature (for example, 2 ° C. or less) and the fuel cell 6 body may be frozen, the PG burner is similarly used. The control unit (not shown) sends a signal to the pump 48 to operate the pump 48 to circulate the hot water to the cooling unit 6c of the fuel cell 6 and send the hot water to the cooling unit 6c. Prevents freezing by raising the temperature of the main unit.
【0040】また、固体高分子形燃料電池発電装置GS
1の装置内部の雰囲気の温度を検知する図示しない手段
(温度計)が設定温度以下(例えば2℃以下)になって
上記水系統が凍結する恐れがある場合、同様にしてPG
バーナ34を作動させて上記のように温水を循環すると
ともに図示しない制御装置から信号をポンプ48に送っ
てポンプ48を作動させて燃料電池6の冷却部6cに温
水を循環して送って燃料電池6本体の温度を上昇させて
凍結防止する。Further, the polymer electrolyte fuel cell power generator GS
If the means (thermometer) (not shown) for detecting the temperature of the atmosphere inside the apparatus of 1 is below the set temperature (for example, 2 ° C. or less) and the water system may be frozen, the PG is similarly set.
The burner 34 is operated to circulate the hot water as described above, and a signal is sent from the control device (not shown) to the pump 48 to operate the pump 48 to circulate and send the hot water to the cooling unit 6c of the fuel cell 6. 6 Raise the body temperature to prevent freezing.
【0041】また、上記の例ではプロセスガスバーナ3
4を燃焼させた場合について説明したが、プロセスガス
バーナ34を燃焼させずに貯湯タンク50の温水を前記
水系統の一部あるいは全部に循環して送って凍結防止す
ることもできる。In the above example, the process gas burner 3
Although the case where 4 is burned has been described, the hot water in the hot water storage tank 50 may be circulated and sent to part or all of the water system without burning the process gas burner 34 to prevent freezing.
【0042】そして、水タンク21の水温(前記温度計
T2で測定される水温)が例えば10℃以上になった場
合は図示しない制御装置から信号をPGバーナ34、フ
ァン37、ポンプP(排熱回収用ポンプ)などへ送っ
て、これらを停止する。このように間欠的にポンプP、
PGバーナ34、ファン37などを作動させることによ
り水系統の凍結を防止できる。When the water temperature of the water tank 21 (water temperature measured by the thermometer T2) becomes, for example, 10 ° C. or higher, signals are sent from the controller (not shown) to the PG burner 34, the fan 37, the pump P (exhaust heat). (Collection pump) and stop these. In this way, the pump P is intermittently
It is possible to prevent freezing of the water system by operating the PG burner 34, the fan 37, and the like.
【0043】(本発明の固体高分子形燃料電池発電装置
GS1の停止時、貯湯タンク50を含む水系統中の水が
凍結する恐れがある場合)水タンク21の水温(温度計
T2で常時監視して測定される水温)は設定温度以上
(例えば2℃以上)であるが、貯湯タンク50を含む水
系統に設置した図示しない温度計で常時監視して測定さ
れる水温が設定温度以下(例えば2℃以下)になって凍
結する恐れがある場合、図示しない制御装置から信号を
PGバーナ34、ファン37、開閉弁81、82、ポン
プPに送って、ファン37を作動させ、PGバーナ34
を作動させて点火するとともに、ラインL2の開閉弁8
1を開け、ラインL1の開閉弁82を閉め、そしてポン
プPを作動させて、PGバーナ34に連結された熱交換
器46で熱回収された温水Aを貯湯タンク50に循環し
て送って、貯湯タンク50を含む水系統中の水を加熱す
る(図3参照。太実線で温水の流れを示す。開閉弁8
1、82の開閉状態、ファン37およびPGバーナ34
の作動状況を図3中の表に示す)。(When the polymer electrolyte fuel cell power generator GS1 of the present invention is stopped, water in the water system including the hot water storage tank 50 may freeze) Water temperature of the water tank 21 (always monitored by the thermometer T2) The water temperature measured by the above is equal to or higher than the set temperature (for example, 2 ° C. or higher), but the water temperature constantly monitored and measured by a thermometer (not shown) installed in the water system including the hot water storage tank 50 is equal to or lower than the set temperature (for example, When there is a risk of freezing due to (2 ° C. or less), a signal is sent from the control device (not shown) to the PG burner 34, the fan 37, the on-off valves 81 and 82, and the pump P to operate the fan 37, and the PG burner 34
And ignites, and the on-off valve 8 of the line L2
1 is opened, the on-off valve 82 of the line L1 is closed, and the pump P is operated to circulate the hot water A recovered by the heat exchanger 46 connected to the PG burner 34 to the hot water storage tank 50, The water in the water system including the hot water storage tank 50 is heated (see FIG. 3. The thick solid line indicates the flow of hot water. The on-off valve 8
1, 82 open / closed state, fan 37 and PG burner 34
The operating status of is shown in the table in FIG. 3).
【0044】そして、貯湯タンク50を含む水系統中の
水温が例えば10℃以上になった場合は図示しない制御
装置から信号をPGバーナ34、ファン37へ送って、
これらを停止する。このように間欠的にポンプP、PG
バーナ34、ファン37を作動させることにより水系統
の凍結を防止できる。Then, when the water temperature in the water system including the hot water storage tank 50 becomes, for example, 10 ° C. or higher, a signal is sent from the control device (not shown) to the PG burner 34 and the fan 37,
Stop these. In this way, the pumps P, PG are intermittently
The freezing of the water system can be prevented by operating the burner 34 and the fan 37.
【0045】なお、上記実施形態の説明は、本発明を説
明するためのものであって、特許請求の範囲に記載の発
明を限定し、或は範囲を減縮するものではない。又、本
発明の各部構成は上記実施形態に限らず、特許請求の範
囲に記載の技術的範囲内で種々の変形が可能である。The above description of the embodiments is for explaining the present invention and does not limit the invention described in the claims or reduce the scope thereof. Further, the configuration of each part of the present invention is not limited to the above embodiment, and various modifications can be made within the technical scope described in the claims.
【0046】[0046]
【発明の効果】本発明の請求項1記載の固体高分子形燃
料電池発電装置は、燃料電池のメンテナンスが簡略化さ
れ、発電と熱利用のコジェネレーションシステムの形態
をとるので、燃料電池の発電効率が図られるばかりでな
く、このシステムで使用される水の有効な再利用が図ら
れる効果があるとともに、装置停止時における水系統の
凍結を自動的に防止して、凍結により水タンク、燃料電
池、貯湯タンク、水系統の熱交換器類、配管類、弁類、
ポンプ類、パイプ類などが損傷を受けるのを防止でき、
寒冷地や冬季における保守作業を省くことができ、装置
寿命が向上して信頼性が高くなるなどの顕著な効果を奏
する。The polymer electrolyte fuel cell power generator according to claim 1 of the present invention simplifies the maintenance of the fuel cell and takes the form of a cogeneration system for power generation and heat utilization. Not only the efficiency is improved, but also the water used in this system is effectively reused, and the water system is automatically prevented from freezing when the equipment is stopped. Batteries, hot water storage tanks, water system heat exchangers, piping, valves,
Prevents damage to pumps, pipes, etc.
Maintenance work in cold regions and winters can be omitted, and the remarkable effects such as improved device life and higher reliability are achieved.
【0047】本発明の請求項2記載の固体高分子形燃料
電池発電装置は、請求項1記載の固体高分子形燃料電池
発電装置と同じ作用効果を奏するとともに、前記プロセ
スガスバーナを燃焼させずに装置停止時における水系統
の凍結を自動的に容易に防止できるという顕著な効果を
奏する。A polymer electrolyte fuel cell power generator according to a second aspect of the present invention has the same effects as the polymer electrolyte fuel cell power generator according to the first aspect, and does not burn the process gas burner. The remarkable effect is that the freezing of the water system can be automatically and easily prevented when the apparatus is stopped.
【0048】本発明の請求項3記載の固体高分子形燃料
電池発電装置は、請求項1記載の固体高分子形燃料電池
発電装置と同じ作用効果を奏するとともに、燃料電池の
冷却部に冷却水を送るポンプを作動させ、前記水タンク
内の水を循環して燃料電池本体を暖めて凍結を防止する
ので、凍結により燃料電池本体が損傷を受けるのをより
効果的に防止できるという顕著な効果を奏する。The polymer electrolyte fuel cell power generator according to claim 3 of the present invention has the same effects as the polymer electrolyte fuel cell power generator according to claim 1, and cooling water for the cooling portion of the fuel cell. The fuel cell main body is warmed by circulating the water in the water tank to prevent it from freezing, so that the fuel cell main body can be more effectively prevented from being damaged by freezing. Play.
【0049】本発明の請求項4記載の固体高分子形燃料
電池発電装置は、請求項1記載の固体高分子形燃料電池
発電装置と同じ作用効果を奏するとともに、前記水タン
クあるいは燃料電池本体の温度がある定められた温度以
上になると、前記プロセスガスバーナの燃焼を行ってい
る場合はそれを停止し、かつ排熱回収用ポンプを停止す
るので、凍結防止に必要なエネルギーを必要最小限に留
めることができるという顕著な効果を奏する。A polymer electrolyte fuel cell power generator according to a fourth aspect of the present invention has the same effects as the polymer electrolyte fuel cell power generator according to the first aspect, and at the same time, the water tank or the fuel cell main body When the temperature exceeds a specified temperature, the process gas burner is stopped if it is burning, and the exhaust heat recovery pump is stopped, so the energy required to prevent freezing is kept to the minimum necessary. It has a remarkable effect of being able to.
【0050】本発明の請求項5記載の固体高分子形燃料
電池発電装置は、請求項1記載の固体高分子形燃料電池
発電装置と同じ作用効果を奏するとともに、凍結を検知
する手段が前記水タンクの温度を検知する手段であり、
水タンクの温度がある定められた値以下になった場合
に、前記プロセスガスバーナを燃焼させて前記貯湯タン
クの温水を昇温し前記水系統の一部あるいは全部に循環
して送って凍結防止するので、凍結により水タンクおよ
び前記水系統が損傷を受けるのをより効率的に防止でき
るという顕著な効果を奏する。The polymer electrolyte fuel cell power generator according to claim 5 of the present invention has the same effects as the polymer electrolyte fuel cell power generator according to claim 1, and the means for detecting freezing is the water. Is a means to detect the temperature of the tank,
When the temperature of the water tank falls below a predetermined value, the process gas burner is burned to raise the hot water in the hot water storage tank and is circulated to part or all of the water system to be sent to prevent freezing. Therefore, it is possible to more effectively prevent the water tank and the water system from being damaged by freezing.
【0051】本発明の請求項6記載の固体高分子形燃料
電池発電装置は、請求項1記載の固体高分子形燃料電池
発電装置と同じ作用効果を奏するとともに、凍結を検知
する手段が燃料電本体の温度を検知する手段であり、燃
料電池本体の温度がある定められた値以下になった場合
に、前記プロセスガスバーナを燃焼させて前記貯湯タン
クの温水を昇温し前記水系統の一部あるいは全部に循環
して送って凍結防止するので、凍結により燃料電本体お
よび前記水系統が損傷を受けるのをより効率的に防止で
きるという顕著な効果を奏する。The polymer electrolyte fuel cell power generator according to claim 6 of the present invention has the same effects as the polymer electrolyte fuel cell power generator according to claim 1, and the means for detecting freezing is the fuel cell. It is a means for detecting the temperature of the main body, and when the temperature of the main body of the fuel cell becomes lower than a predetermined value, the process gas burner is burned to raise the hot water in the hot water storage tank and a part of the water system. Alternatively, since it is circulated and sent to all to prevent freezing, there is a remarkable effect that it is possible to more efficiently prevent damage to the fuel cell body and the water system due to freezing.
【0052】本発明の請求項7記載の固体高分子形燃料
電池発電装置は、請求項1記載の固体高分子形燃料電池
発電装置と同じ作用効果を奏するとともに、凍結を検知
する手段が固体高分子形燃料電池発電装置内の雰囲気の
温度を検知する手段であり、前記雰囲気の温度がある定
められた値以下になった場合に、前記プロセスガスバー
ナを燃焼させて前記貯湯タンクの温水を昇温し前記水系
統の一部あるいは全部に循環して送って凍結防止するの
で、凍結により燃料電本体および前記水系統などが損傷
を受けるのをより効率的に防止できるという顕著な効果
を奏する。The polymer electrolyte fuel cell power generator according to claim 7 of the present invention has the same effects as the polymer electrolyte fuel cell power generator according to claim 1, and the means for detecting freezing has a solid height. A means for detecting the temperature of the atmosphere in the molecular fuel cell power generator, and when the temperature of the atmosphere becomes a predetermined value or less, the process gas burner is burned to raise the hot water in the hot water storage tank. However, since it is circulated and sent to part or all of the water system to prevent freezing, there is a remarkable effect that it is possible to more efficiently prevent damage to the fuel cell body and the water system due to freezing.
【図1】本発明による固体高分子形燃料電池発電装置の
一実施形態を示す系統図である。FIG. 1 is a system diagram showing one embodiment of a polymer electrolyte fuel cell power generator according to the present invention.
【図2】図1に示した本発明による固体高分子形燃料電
池発電装置の凍結防止のための温水の流れの一実施形態
を示す説明図である。FIG. 2 is an explanatory view showing an embodiment of a flow of hot water for preventing freezing of the polymer electrolyte fuel cell power generator according to the present invention shown in FIG.
【図3】図1に示した本発明による固体高分子形燃料電
池発電装置の凍結防止のための温水の流れの他の実施形
態を示す説明図である。FIG. 3 is an explanatory view showing another embodiment of the flow of hot water for preventing freezing of the polymer electrolyte fuel cell power generator according to the present invention shown in FIG. 1.
【図4】従来の固体高分子形燃料電池発電装置の系統図
である。FIG. 4 is a system diagram of a conventional polymer electrolyte fuel cell power generator.
3 改質器
4 CO変成器
5 CO除去器
6 燃料電池
6c 冷却部
10、23〜25、28、43、47、48 ポンプ
21 水タンク
34 プロセスガスバーナ
17、18、19、32、71 熱交換器
37 プロセスガスバーナに燃焼用空気を送るファン
46 プロセスガスバーナに連結された熱交換器
50 貯湯タンク
L1 温水Aを熱交換可能に水タンクへ循環して送るラ
イン
L2 温水Aを貯湯タンクへ送るライン
GS、GS1 固体高分子形燃料電池発電装置
RD、RD1 熱回収装置
HEX 熱交換器
T1、T2 温度計
P 排熱回収用ポンプ3 reformer 4 CO shifter 5 CO remover 6 fuel cell 6c cooling unit 10, 23 to 25, 28, 43, 47, 48 pump 21 water tank 34 process gas burner 17, 18, 19, 32, 71 heat exchanger 37 Fan for sending combustion air to the process gas burner 46 Heat exchanger 50 connected to the process gas burner 50 Hot water storage tank L1 Line L2 for circulating hot water A to the water tank in a heat exchangeable manner, Line GS for sending hot water A to the hot water storage tank, GS1 polymer electrolyte fuel cell power generator RD, RD1 heat recovery device HEX heat exchangers T1, T2 thermometer P exhaust heat recovery pump
───────────────────────────────────────────────────── フロントページの続き (72)発明者 田島 一弘 大阪府守口市京阪本通2丁目5番5号 三洋電機株式会社内 (72)発明者 山本 聡史 大阪府守口市京阪本通2丁目5番5号 三洋電機株式会社内 (56)参考文献 特開 平8−273689(JP,A) 特開2000−251915(JP,A) 特開 昭64−59776(JP,A) 特開 平11−214025(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 8/00 - 8/24 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Kazuhiro Tajima 2-5-5 Keihan Hondori, Moriguchi-shi, Osaka Sanyo Electric Co., Ltd. (72) Satoshi Yamamoto 2-5 Keihan-hondori, Moriguchi-shi, Osaka No. 5 within Sanyo Electric Co., Ltd. (56) Reference JP-A-8-273689 (JP, A) JP-A-2000-251915 (JP, A) JP-A-64-59776 (JP, A) JP-A-11-214025 (JP, A) (58) Fields surveyed (Int.Cl. 7 , DB name) H01M 8/00-8/24
Claims (7)
G、ブタンなどの燃料ガスを水素に改質する改質器と、
一酸化炭素を変成するCO変成器と、一酸化炭素を除去
するCO除去器と、起動時に各反応器が安定するまで水
素を燃焼するプロセスガスバーナと、水素によって発電
する燃料電池と、燃料電池を冷却するための水を収納し
た水タンクと、前記改質器、燃料電池、プロセスガスバ
ーナなどの排ガスの熱を回収して温水とする熱交換器
と、この温水を蓄える貯湯タンクとを備えた固体高分子
形燃料電池発電装置であって、 装置停止時に水系統が凍結する恐れがある場合は、それ
を検知して前記プロセスガスバーナを燃焼させて前記貯
湯タンクの温水を昇温し前記水系統の一部あるいは全部
に循環して送って凍結防止する制御システムを備えたこ
とを特徴とする固体高分子形燃料電池発電装置。1. Natural gas, city gas, methanol, LP
A reformer for reforming a fuel gas such as G or butane into hydrogen,
A CO shifter that transforms carbon monoxide, a CO remover that removes carbon monoxide, a process gas burner that burns hydrogen until each reactor stabilizes at startup, a fuel cell that generates electricity using hydrogen, and a fuel cell. A solid body that includes a water tank that stores water for cooling, a heat exchanger that recovers heat of exhaust gas from the reformer, fuel cell, process gas burner, and the like into hot water, and a hot water storage tank that stores the hot water. In a polymer electrolyte fuel cell power generator, if there is a risk that the water system will freeze when the device is stopped, it is detected and the process gas burner is burned to raise the hot water in the hot water storage tank to raise the temperature of the water system. A polymer electrolyte fuel cell power generation device comprising a control system for circulating and sending a part or all of it to prevent freezing.
G、ブタンなどの燃料ガスを水素に改質する改質器と、
一酸化炭素を変成するCO変成器と、一酸化炭素を除去
するCO除去器と、起動時に各反応器が安定するまで水
素を燃焼するプロセスガスバーナと、水素によって発電
する燃料電池と、燃料電池を冷却するための水を収納し
た水タンクと、前記改質器、燃料電池、プロセスガスバ
ーナなどの排ガスの熱を回収して温水とする熱交換器
と、この温水を蓄える貯湯タンクとを備えた固体高分子
形燃料電池発電装置であって、 装置停止時に水系統が凍結する恐れがある場合は、それ
を検知して前記プロセスガスバーナを燃焼させずに前記
貯湯タンクの温水を前記水系統の一部あるいは全部に循
環して送って凍結防止する制御システムを備えたことを
特徴とする固体高分子形燃料電池発電装置。2. Natural gas, city gas, methanol, LP
A reformer for reforming a fuel gas such as G or butane into hydrogen,
A CO shifter that transforms carbon monoxide, a CO remover that removes carbon monoxide, a process gas burner that burns hydrogen until each reactor stabilizes at startup, a fuel cell that generates electricity using hydrogen, and a fuel cell. A solid body that includes a water tank that stores water for cooling, a heat exchanger that recovers heat of exhaust gas from the reformer, fuel cell, process gas burner, and the like into hot water, and a hot water storage tank that stores the hot water. In a polymer electrolyte fuel cell power generator, if there is a risk that the water system will freeze when the device is stopped, it is detected and hot water in the hot water storage tank is used as a part of the water system without burning the process gas burner. Alternatively, the polymer electrolyte fuel cell power generator is provided with a control system for circulating and sending the whole to prevent freezing.
を作動させ、前記水タンク内の水を循環して燃料電池本
体を暖めて凍結を防止することを特徴とする請求項1あ
るいは請求項2記載の固体高分子形燃料電池発電装置。3. The method according to claim 1, wherein a pump for supplying cooling water to the cooling portion of the fuel cell is operated to circulate the water in the water tank to warm the fuel cell main body to prevent freezing. Item 2. A polymer electrolyte fuel cell power generator according to item 2.
度がある定められた温度以上になると、前記プロセスガ
スバーナの燃焼を行っている場合はそれを停止し、かつ
排熱回収用ポンプを停止することを特徴とする請求項1
から請求項3のいずれかに記載の固体高分子形燃料電池
発電装置。4. When the temperature of the water tank or the fuel cell main body exceeds a predetermined temperature, the process gas burner is stopped if it is burning and the exhaust heat recovery pump is stopped. Claim 1 characterized by the above-mentioned.
4. The polymer electrolyte fuel cell power generator according to claim 3.
度を検知する手段であり、水タンクの温度がある定めら
れた値以下になった場合に、前記プロセスガスバーナを
燃焼させて前記貯湯タンクの温水を昇温し前記水系統の
一部あるいは全部に循環して送って凍結防止することを
特徴とする請求項1、請求項3あるいは請求項4記載の
固体高分子形燃料電池発電装置。5. The means for detecting freezing is a means for detecting the temperature of the water tank, and when the temperature of the water tank falls below a predetermined value, the process gas burner is burned to cause the hot water storage tank. The solid polymer fuel cell power generator according to claim 1, 3 or 4, wherein the hot water is heated to circulate and sent to part or all of the water system to prevent freezing.
を検知する手段であり、燃料電池本体の温度がある定め
られた値以下になった場合に、前記プロセスガスバーナ
を燃焼させて前記貯湯タンクの温水を昇温し前記水系統
の一部あるいは全部に循環して送って凍結防止すること
を特徴とする請求項1、請求項3、請求項4あるいは請
求項5記載の固体高分子形燃料電池発電装置。6. The means for detecting freezing is a means for detecting the temperature of the fuel cell main body, and when the temperature of the fuel cell main body falls below a certain value, the process gas burner is burned to store the hot water. The solid polymer form according to claim 1, claim 3, claim 4 or claim 5, wherein the temperature of hot water in the tank is raised and circulated to a part or all of the water system to be sent to prevent freezing. Fuel cell power generator.
電池発電装置内の雰囲気の温度を検知する手段であり、
前記雰囲気の温度がある定められた値以下になった場合
に、前記プロセスガスバーナを燃焼させて前記貯湯タン
クの温水を昇温し前記水系統の一部あるいは全部に循環
して送って凍結防止することを特徴とする請求項1、請
求項3、請求項4、請求項5あるいは請求項6記載の固
体高分子形燃料電池発電装置。7. The means for detecting freezing is a means for detecting the temperature of the atmosphere in the polymer electrolyte fuel cell power generator,
When the temperature of the atmosphere becomes lower than a predetermined value, the process gas burner is burned to raise the temperature of the hot water in the hot water storage tank, and the hot water is circulated and sent to part or all of the water system to prevent freezing. The polymer electrolyte fuel cell power generator according to claim 1, claim 3, claim 4, claim 5, or claim 6, characterized in that.
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001006349A JP3416653B2 (en) | 2001-01-15 | 2001-01-15 | Polymer electrolyte fuel cell power generator |
| US10/221,338 US7052787B2 (en) | 2001-01-12 | 2002-01-09 | Solid high polymer type fuel cell power generating device |
| DE60239591T DE60239591D1 (en) | 2001-01-12 | 2002-01-09 | SOLID HIGH POLYMER FUEL CELL POWER SYSTEM |
| DK02729526.0T DK1351328T3 (en) | 2001-01-12 | 2002-01-09 | Solid high polymer fuel cell energy generating apparatus |
| EP02729526A EP1351328B1 (en) | 2001-01-12 | 2002-01-09 | Solid high polymer type fuel cell power generating device |
| AT02729526T ATE504097T1 (en) | 2001-01-12 | 2002-01-09 | SOLID HIGH POLYMER FUEL CELL POWER SUPPLY SYSTEM |
| PCT/JP2002/000053 WO2002056403A1 (en) | 2001-01-12 | 2002-01-09 | Solid high polymer type fuel cell power generating device |
| KR10-2002-7011981A KR100525538B1 (en) | 2001-01-12 | 2002-01-09 | Solid high polymer type fuel cell power generating device |
| CNB028000706A CN100391037C (en) | 2001-01-12 | 2002-01-09 | Proton exchange membrane fuel cell power generation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001006349A JP3416653B2 (en) | 2001-01-15 | 2001-01-15 | Polymer electrolyte fuel cell power generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002216824A JP2002216824A (en) | 2002-08-02 |
| JP3416653B2 true JP3416653B2 (en) | 2003-06-16 |
Family
ID=18874246
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001006349A Expired - Fee Related JP3416653B2 (en) | 2001-01-12 | 2001-01-15 | Polymer electrolyte fuel cell power generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3416653B2 (en) |
Families Citing this family (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3835357B2 (en) | 2002-06-12 | 2006-10-18 | 株式会社デンソー | Fuel cell system |
| JP4405717B2 (en) * | 2002-09-13 | 2010-01-27 | リンナイ株式会社 | Cogeneration system |
| WO2005112175A1 (en) * | 2004-05-19 | 2005-11-24 | Matsushita Electric Industrial Co., Ltd. | Fuel cell system |
| JP4955913B2 (en) * | 2004-06-11 | 2012-06-20 | 株式会社豊田中央研究所 | Fuel cell system |
| JP4986424B2 (en) * | 2005-08-11 | 2012-07-25 | 京セラ株式会社 | Power generator |
| CN101467293B (en) | 2006-06-06 | 2011-07-27 | 松下电器产业株式会社 | Fuel cell system |
| JP4825704B2 (en) * | 2007-03-09 | 2011-11-30 | トヨタ自動車株式会社 | Fuel cell power generation system and operation method thereof |
| JP5231756B2 (en) * | 2007-06-04 | 2013-07-10 | 株式会社東芝 | Fuel cell power generator and method of operating the same |
| KR101392452B1 (en) | 2007-10-19 | 2014-05-08 | 삼성전자주식회사 | A fuel cell apparatus providing fuel processor and managing method thereof |
| JP4845899B2 (en) * | 2008-01-21 | 2011-12-28 | アイシン精機株式会社 | Fuel cell system |
| JP2009181941A (en) * | 2008-02-01 | 2009-08-13 | Toshiba Corp | Fuel cell system |
| JP5098685B2 (en) * | 2008-02-18 | 2012-12-12 | カシオ計算機株式会社 | Small chemical reactor |
| JP4977151B2 (en) * | 2009-02-06 | 2012-07-18 | トヨタ自動車株式会社 | Fuel cell power generation system and operation method thereof |
| JP5471030B2 (en) * | 2009-05-21 | 2014-04-16 | アイシン精機株式会社 | Fuel cell system |
| JP5068291B2 (en) * | 2009-08-26 | 2012-11-07 | 株式会社Eneosセルテック | Fuel cell system |
| JP6758234B2 (en) * | 2017-03-29 | 2020-09-23 | 京セラ株式会社 | Controls, fuel cell systems, and control methods |
| JP2019091658A (en) * | 2017-11-16 | 2019-06-13 | アイシン精機株式会社 | Fuel cell system |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000251915A (en) | 1999-03-03 | 2000-09-14 | Nissan Motor Co Ltd | Fuel cell system |
-
2001
- 2001-01-15 JP JP2001006349A patent/JP3416653B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000251915A (en) | 1999-03-03 | 2000-09-14 | Nissan Motor Co Ltd | Fuel cell system |
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| Publication number | Publication date |
|---|---|
| JP2002216824A (en) | 2002-08-02 |
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