JPS63298975A - Temperature rising device for air cooled fuel cell - Google Patents

Temperature rising device for air cooled fuel cell

Info

Publication number
JPS63298975A
JPS63298975A JP62133006A JP13300687A JPS63298975A JP S63298975 A JPS63298975 A JP S63298975A JP 62133006 A JP62133006 A JP 62133006A JP 13300687 A JP13300687 A JP 13300687A JP S63298975 A JPS63298975 A JP S63298975A
Authority
JP
Japan
Prior art keywords
temperature
air
fuel cell
cell
combustion gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP62133006A
Other languages
Japanese (ja)
Inventor
Takashi Ouchi
崇 大内
Toshio Hirota
広田 俊夫
Tomoyoshi Kamoshita
友義 鴨下
Takashi Ujiie
氏家 孝
Atsutomo Ooyama
大山 敦智
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
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP62133006A priority Critical patent/JPS63298975A/en
Publication of JPS63298975A publication Critical patent/JPS63298975A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04223Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0267Collectors; Separators, e.g. bipolar separators; Interconnectors having heating or cooling means, e.g. heaters or coolant flow channels
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04223Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
    • H01M8/04225Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells during start-up
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04014Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
    • H01M8/04022Heating by combustion
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04097Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the reactants
    • 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

PURPOSE:To efficiently raise the temperature of a cell with a simple device by installing an air supply means which cools combustion gas to an optimum temperature by normal temperature air sucked from the outside in a supply pipeline of combustion gas for a starting burner. CONSTITUTION:When an air cooled fuel cell 10 is started, a valve 26 is opened, and a blower 9 is operated to suck the air in a starting burner 21, then fuel is supplied to generate combustion gas. The combustion gas is circulated in a supply pipeline 15 with the blower 9 and the temperature of a cell 10 is raised. During this operation, the opening of an air supply valve 27 is adjusted to control the amount of air, and high temperature combustion gas is cooled to a certen temperature which is optimum to raise the temperature of the cell 10. When the temperature of the cell is raised to a specified value, the operation of the burner 21 is stopped and the air supply valve 27 is closed to keep the temperature of the cell constant. The temperature of the cell is efficiently raised with a simple device.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、電解質と隔離された冷却ガス通路に反応ガス
と独立した冷却ガスを供給してなる空冷式燃料電池の昇
温装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a temperature raising device for an air-cooled fuel cell, which supplies a cooling gas independent of a reactant gas to a cooling gas passage isolated from an electrolyte.

〔従来の技術〕[Conventional technology]

燃料電池は燃料の有する化学エネルギーを直接電気エネ
ルギーに変換する装置で、熱効率が高く、騒音、電気的
ノイズや有害排出物が少ないとG)うような利点がある
ために新しい発電装置として注目されている。これは電
解質を挾んだ電極間に燃料と酸化剤を供給することによ
り、化学的に電気を取りだすものであり、発電容量の大
小にかかわらず効尤が高く、分散形の中小規模の発電所
用から可搬形の独立電源用まで、盛んに研児、開発が行
なわれている。
A fuel cell is a device that directly converts the chemical energy of fuel into electrical energy, and has attracted attention as a new power generation device because of its high thermal efficiency, low noise, electrical noise, and low harmful emissions. ing. This system extracts electricity chemically by supplying fuel and oxidizer between electrodes that sandwich an electrolyte, and is highly effective regardless of the size of the power generation capacity, and is suitable for small and medium-sized distributed power plants. Research and development is being actively conducted on everything from portable independent power sources.

燃料電池は反応ガスの供給tこより”[池反応を起こさ
せて運転されるが、V屓反応時発生する熱を除去して運
転温度に保持するために携料電池本体を冷却している。
A fuel cell is operated by causing a reaction to occur due to the supply of reactant gas, but the main body of the portable cell is cooled to remove the heat generated during the reaction and maintain the operating temperature.

この冷却構造には空冷式と液冷式とがあるが、特に小容
量の独′s1.″Bt源用としては、システム構成の簡
潔な空冷式の方が有利である。
There are two types of cooling structures: air-cooled and liquid-cooled. ``As a Bt source, an air-cooled type with a simple system configuration is more advantageous.

燃料電池に供給する反応ガスは酸化剤として空気が、ま
た燃料として一般に改質原料を水素番こ富むガスに数置
する溶料改質器からの改質ガスが使用されており、燃料
電池と・納料改質器とを組合わせて燃料゛α池発電装置
を構成して発電が行なわれる。なオd懲料改質器の燃焼
用燃料は燃料電池から排出される未反応水素を含むオフ
ガスが使用される。
The reaction gas supplied to the fuel cell is air as an oxidant, and the fuel is reformed gas from a solvent reformer in which the reforming raw material is generally placed in a hydrogen-rich gas. - Power is generated by combining it with a feed reformer to form a fuel α-cell power generation device. The off-gas containing unreacted hydrogen discharged from the fuel cell is used as the fuel for combustion in the reformer.

ところで空冷式燃料電池を効率よく運転するには、例え
ばりん酸形の場合には電池の運転温度を通常190″C
程度(こ保持して運転されるが、停止状怒から起動する
場合には、改質ガス中の少量の一酸化炭素が電池の電極
触媒に悪影響を及+1さない程度、例えば140℃程度
以上に電池を昇温しなけ几ばならない。このため空冷式
燃料電池には昇温に必要な起動装置を備えている。
By the way, in order to operate an air-cooled fuel cell efficiently, for example, in the case of a phosphoric acid type fuel cell, the operating temperature of the cell is usually 190"C.
(It is operated with this condition maintained, but when starting from a stop condition, the temperature must be maintained to the extent that a small amount of carbon monoxide in the reformed gas does not adversely affect the electrode catalyst of the battery, e.g. 140℃ or higher. It is necessary to raise the temperature of the battery.For this reason, air-cooled fuel cells are equipped with a starting device necessary for raising the temperature.

このような構成の空冷式燃料電池発電装置の系統図を第
2図に示す。図において1は燃料改質器であり、改質原
料としてのメタノール等の液体燃料が外部から気化器2
に送液され、バーナ3で燃焼した燃焼ガスにより加熱さ
れて気化し、この気化ガスは改質触媒が充填された反応
器4にて、バーナ3からの燃焼ガスにより加熱されて水
素に富むカスに改質され、この改質ガスが燃料供給管路
5を経て空冷式の燃料電池10の燃料電極11に供給さ
れる。なお、バーナ3では燃焼空気用ブロワ6により送
気される燃焼空気とオフガス供給管路7を経て燃料電池
10の燃料電極1]から供給されるオフガスとにより・
−焼が行なわれる。
A system diagram of an air-cooled fuel cell power generating apparatus having such a configuration is shown in FIG. In the figure, 1 is a fuel reformer, and liquid fuel such as methanol as a reforming raw material is supplied from the outside to a vaporizer 2.
The vaporized gas is heated by the combustion gas from the burner 3 and vaporized, and this vaporized gas is heated by the combustion gas from the burner 3 in the reactor 4 filled with a reforming catalyst to form hydrogen-rich scum. This reformed gas is supplied to the fuel electrode 11 of the air-cooled fuel cell 10 via the fuel supply pipe 5. In addition, in the burner 3, the combustion air supplied by the combustion air blower 6 and the off-gas supplied from the fuel electrode 1 of the fuel cell 10 via the off-gas supply pipe 7
- Burning takes place.

空冷式・燃料電池10は燃料電極11に前述の改質ガス
が供給され、酸化剤電極12に反応ガス用空気ブロワ8
により空気が供給されて運転され、電池反応により電気
を発生する。13は熱媒体通路(運転時には冷却媒体通
路となる)を有する冷却板であり、冷却板13を経由し
、冷却、加熱用ブロワ9を備えた循環管路15を設け、
冷却板13の出口部に循環管路15から分岐する排出管
16とブロワ9の吸込部に調整弁18を備えた吸込管1
7とが設けらV、ている。なおブロワ9の吐出部に加熱
用ヒータ19を設け、ブロワ9から吐出される空気を加
熱するようにしている。
In the air-cooled fuel cell 10, the above-mentioned reformed gas is supplied to the fuel electrode 11, and an air blower 8 for reactant gas is supplied to the oxidizer electrode 12.
It is operated by supplying air and generates electricity through battery reactions. Reference numeral 13 denotes a cooling plate having a heat medium passage (which becomes a cooling medium passage during operation), and a circulation pipe 15 equipped with a blower 9 for cooling and heating is provided via the cooling plate 13.
A suction pipe 1 equipped with a discharge pipe 16 branching from the circulation pipe 15 at the outlet of the cooling plate 13 and a regulating valve 18 at the suction part of the blower 9.
7 is provided. Note that a heating heater 19 is provided at the discharge portion of the blower 9 to heat the air discharged from the blower 9.

このような構成により空冷式燃料電池lOを起動するに
は、前述のように電極触媒の被毒作用をさけるために燃
料電池本体を昇温、例えばりん酸形の場合t4o’ca
度に昇温する必要があるので、ブロワ9を駆動し、調整
弁18を適量の弁開度にして空気を吸込んで冷却板13
に送気するとともに加熱ヒータ19によりこの空気を加
熱して熱媒体としての熱風にして冷却板13ζこ送気し
て・−料N、池本体を所定温度まで昇温する。熱風は循
環管路15を循還して流れるとともに調整弁18から吸
気された空気量と同量が排出管16から排出されるよう
に排出管16に設けられた図示しない排出ダンパの開度
を調整する。なお、熱風の循環流量は排出流量の数倍程
度にして冷却板13にての伝熱熱風量を多くして燃料電
池本体が均等に昇温できるようにしている。
In order to start up an air-cooled fuel cell lO with such a configuration, the temperature of the fuel cell main body must be increased to avoid poisoning of the electrode catalyst as described above.For example, in the case of a phosphoric acid type fuel cell, the temperature must be increased to
Since it is necessary to raise the temperature to approximately
At the same time, the air is heated by the heater 19 to become hot air as a heat medium, and the air is sent to the cooling plate 13ζ to raise the temperature of the pond body to a predetermined temperature. The hot air circulates and flows through the circulation pipe 15, and the opening degree of a discharge damper (not shown) provided in the discharge pipe 16 is adjusted so that the same amount of air as taken in from the regulating valve 18 is discharged from the discharge pipe 16. adjust. Note that the circulating flow rate of the hot air is set to several times the discharge flow rate to increase the amount of heat-transferring hot air at the cooling plate 13 so that the temperature of the fuel cell body can be raised evenly.

昇温か完了すれば・燃料改質器1からの改質ガスと反応
ガス用空気ブロワ8からの空気がそれぞれ燃料電池10
の燃料電極11と酸化剤電極12とに供給され燃料電池
の運転が行なわれる。なお燃料電池の運転時の冷却は加
熱ヒータ19を停止して循環管路15に空気を循環する
ことにより行なわれる。
When the temperature rise is completed, the reformed gas from the fuel reformer 1 and the air from the reaction gas air blower 8 are respectively supplied to the fuel cell 10.
The fuel is supplied to the fuel electrode 11 and the oxidizer electrode 12 to operate the fuel cell. Note that the fuel cell is cooled during operation by stopping the heater 19 and circulating air through the circulation pipe 15.

第3図は燃料電池本体を昇温する異なる従来例であり、
図において循環管路15の途中(こ熱交換器筒を介挿装
着し、熱交換器筒の伝熱管筒aに起動用バーナ2]の燃
焼ガスが供給されるようにしている。起動用バーナ2】
には図示しない燃料供給管からの燃料改質器1の液体原
料等の燃料と燃焼空気用ブロワnにより送気される空気
とが供給されるようにしている。
Figure 3 shows a different conventional example of increasing the temperature of the fuel cell body.
In the figure, the combustion gas from the starting burner 2 is supplied to the heat exchanger tube a of the heat exchanger tube in the middle of the circulation pipe 15 (a heat exchanger tube is inserted and attached to the starting burner 2). 2]
Fuel such as a liquid raw material for the fuel reformer 1 is supplied from a fuel supply pipe (not shown) and air supplied by a combustion air blower n.

このような構成により熱風は第2図の従来例と同じ要領
で循還管路15を循環し、熱風は熱交換器筒にて伝熱管
20aを流れる起動用バーナ21からの燃焼ガスにより
加熱され、冷却板13を介して燃料電池本体を昇温する
With this configuration, the hot air circulates through the circulation pipe 15 in the same manner as in the conventional example shown in FIG. , the temperature of the fuel cell body is raised via the cooling plate 13.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

空冷式燃料電池の起動時打なう昇温に際して循環管路1
5に加熱ヒータ19を設けて循還する空気を加熱して熱
風を得る方法は加熱ヒータ19等からなる補機に供給す
る電力が太きいため、補助電源が大型化するという欠点
がある。また、循環管路15に熱交換器筒を介挿装着し
、起動用バーナ21からの燃焼ガスにより伝熱管を介し
て熱交換することにより循環する空気を加熱して熱風を
得る方法はガスとガスとの熱交換であるため熱交換器が
大型になるという欠点がある。
When the temperature rises during startup of the air-cooled fuel cell, the circulation pipe 1
The method of obtaining hot air by providing a heater 19 in the heater 19 and heating the circulating air requires a large amount of power to be supplied to the auxiliary equipment including the heater 19 and the like, which has the disadvantage that the auxiliary power source becomes large. In addition, a method of inserting a heat exchanger cylinder into the circulation pipe line 15 and exchanging heat with the combustion gas from the starting burner 21 through the heat transfer tube to heat the circulating air and obtain hot air is a gas method. Since heat exchange is performed with gas, the disadvantage is that the heat exchanger becomes large.

本発明の目的は空冷式燃料電池の起動時1こ行なう昇温
を簡単な装置により効率よく行なうことのできる昇温装
置を提供することである。
An object of the present invention is to provide a temperature raising device that can efficiently raise the temperature of an air-cooled fuel cell once upon startup using a simple device.

〔問題点を解決するための手段〕[Means for solving problems]

上記問題点を解決するために1本発明によれば電解質と
隔離され、反応ガスと独文した熱媒体が供給される熱i
体通路を有する燃料電池を、前記熱媒体通路にブロワを
有する供給管路を経て供給して昇温する空冷式燃料電池
の昇温装置において、前記ブロワ吸込側の供給管路に前
記熱媒体を供給する起動用バーナと該バーナからの熱媒
体に空気を混合する空気供給手段とを設けるものとする
In order to solve the above problems, according to the present invention, heat i is isolated from the electrolyte and supplied with a reaction gas and a heat transfer medium.
In the heating device for an air-cooled fuel cell that heats up a fuel cell having a body passage by supplying the heat medium passage to the heat medium passage through a supply pipe line having a blower, the heat medium is supplied to the supply pipe line on the blower suction side. A starting burner for supplying air and an air supply means for mixing air with the heat medium from the burner shall be provided.

〔作用〕[Effect]

空冷式燃料電池の昇温のため熱媒体通路に供給される熱
媒体を起動用バーナでの燃料の燃焼による燃焼ガスを使
用するが、燃焼ガスは高温のため、供給管路に設けた空
気供給手段により大気から吸込んだ常温の空気により燃
焼ガスを冷却して燃料電池の昇温に適した温度にする。
To raise the temperature of an air-cooled fuel cell, combustion gas from the combustion of fuel in a startup burner is used as the heat medium supplied to the heat medium passage, but since the combustion gas is high temperature, an air supply installed in the supply pipe is used. The combustion gas is cooled by room-temperature air sucked in from the atmosphere to a temperature suitable for raising the temperature of the fuel cell.

〔実施例〕〔Example〕

以下図面に基づいて本発明の実施例について説明する。 Embodiments of the present invention will be described below based on the drawings.

第1図は本発明の実施例1こよる昇温装置を備えた空冷
式燃料電池発電装置の系統図であり、第2図、第3図の
従来例と同一部品1こは同じ符号を付し、その説明を省
略する。第1図において供給管路である循環管路15に
設けられた冷却、加熱用ブロワ9の吸込側に管路別を介
して起動用バーナ21を設け、起動用バーナ21での燃
料の燃焼によ跨 る燃焼ガスは管雅冴を経て循m管路15に送気されるよ
うにしている。なお26は起動用バーナ21に燃焼空気
を供給する弁である。また管路24から分岐した管路5
に空気供給手段としての′A整弁rを設けている。
FIG. 1 is a system diagram of an air-cooled fuel cell power generation system equipped with a temperature raising device according to Embodiment 1 of the present invention, and the same parts as those in the conventional example shown in FIGS. 2 and 3 are given the same reference numerals. Therefore, the explanation thereof will be omitted. In FIG. 1, a starting burner 21 is provided via a separate pipe on the suction side of the cooling/heating blower 9 provided in the circulation pipe 15 which is a supply pipe, and the starting burner 21 is used to burn fuel. The combustion gas crossing the pipe is sent to the circulation pipe 15 via a pipe. Note that 26 is a valve that supplies combustion air to the starting burner 21. In addition, a pipe line 5 branched from the pipe line 24
A regulating valve 'A' is provided as an air supply means.

このような構成により、空冷式燃料電池10を停止状態
から始動する場合(こけ、弁2Gを開状態にしてブロワ
9を駆動して起動用バーナ21に燃焼空気としての大気
を吸込ませる状態にする。そして図示しない燃料供給管
路からメタノールのような燃料を起動用バーナ21に送
り、吸込まれた燃焼空気により燃料を燃焼させ燃焼ガス
を発生させる。この燃焼ガスは管路Uを経てブロワ9に
吸込まれて循環管路15を循環して燃料電池10を昇温
する。この際調整弁nの弁開度を調整して大気を管路6
を経て吸込ませ、燃焼ガスを冷却して燃料電池10を昇
温するに適した温度にして燃料電池10を昇温する。こ
れは燃焼ガスが高温であり、例えばメタノールを空燃比
1,2〜1.5で燃焼させると素焼ガスの温度は500
℃以上となって排出されるので、これを調整弁nから吸
入した常温の空気により冷却して燃料電池10を構成す
る部材の耐熱温度、例えばりん酸形の場合約200℃を
考慮して燃焼ガスの温度を200℃以下にするためであ
る。
With this configuration, when starting the air-cooled fuel cell 10 from a stopped state (when starting the air-cooled fuel cell 10 from a stopped state), the valve 2G is opened and the blower 9 is driven to cause the starting burner 21 to suck atmospheric air as combustion air. Then, a fuel such as methanol is sent from a fuel supply pipe (not shown) to the starting burner 21, and the fuel is combusted by the intake combustion air to generate combustion gas.This combustion gas is sent to the blower 9 through the pipe U. The atmospheric air is sucked in and circulated through the circulation pipe 15 to raise the temperature of the fuel cell 10.At this time, the opening degree of the regulating valve n is adjusted so that the atmosphere is passed through the pipe 6.
The combustion gas is cooled to a temperature suitable for raising the temperature of the fuel cell 10, and the temperature of the fuel cell 10 is raised. This is because the combustion gas has a high temperature. For example, when methanol is burned at an air-fuel ratio of 1.2 to 1.5, the temperature of the bisque gas is 500.
℃ or higher, so it is cooled by room-temperature air sucked in from the regulating valve n and combusted, taking into account the heat resistance temperature of the components that make up the fuel cell 10, for example, about 200℃ in the case of phosphoric acid type. This is to keep the gas temperature below 200°C.

なお、燃料電池10が所定温度まで昇温したら起動用バ
ーナ21を停止し、弁26.調整弁nを閉にして燃料電
池の温度を一定に保つようにする。
Note that when the temperature of the fuel cell 10 rises to a predetermined temperature, the starting burner 21 is stopped, and the valve 26. Adjustment valve n is closed to keep the temperature of the fuel cell constant.

〔発明の効果〕〔Effect of the invention〕

以上の説明で明らかなようlこ、本発明によれば空冷式
燃料電池の昇温を起動用バーナからの燃焼ガスで行ない
、かつ空気供給手段により常温の空気を供給して高温の
燃焼ガスを冷却して燃料電池の昇温に適した温度にして
昇温を行なうようにしたので、簡単な装置により効率よ
(燃料電池を昇温できる。
As is clear from the above explanation, according to the present invention, the temperature of the air-cooled fuel cell is raised by the combustion gas from the startup burner, and the air supply means supplies room-temperature air to supply high-temperature combustion gas. Since the temperature is increased by cooling the fuel cell to a temperature suitable for raising the temperature of the fuel cell, the temperature of the fuel cell can be raised efficiently using a simple device.

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

第1図は本発明の実施例による昇温装置を備えた空冷式
燃料電池発電装置の系統図、第2図は従来の昇温装置を
備えた空冷式燃料電池発電装置の系統図、第3図は従来
の異なる昇温装置を備えた空冷式燃料電池発電装置の系
統図である。 1:燃料改質器、9ニブ6ワ、10:空冷式燃料電池、
13:熱媒体通路を備えた冷却板、15:供給管路、2
1:起動用バーナ、27=空気供給手段としての調整弁
FIG. 1 is a system diagram of an air-cooled fuel cell power generation device equipped with a temperature raising device according to an embodiment of the present invention, FIG. 2 is a system diagram of an air-cooled fuel cell power generation device equipped with a conventional temperature raising device, and FIG. The figure is a system diagram of an air-cooled fuel cell power generation device equipped with a different conventional temperature raising device. 1: Fuel reformer, 9 nibs, 6 wa, 10: Air-cooled fuel cell,
13: Cooling plate with heat medium passage, 15: Supply pipe line, 2
1: Starting burner, 27 = Regulating valve as air supply means.

Claims (1)

【特許請求の範囲】[Claims] 電解質と隔離され、反応ガスと独立した熱媒体が供給さ
れる熱媒体通路を有する燃料電池を、前記熱媒体通路に
ブロワを有する供給管路を経て熱媒体を供給して昇温す
る空冷式燃料電池の昇温装置において、前記ブロワ吸込
側の供給管路に前記熱媒体を供給する起動用バーナと、
該バーナからの熱媒体に空気を混合する空気供給手段と
を設けたことを特徴とする空冷式燃料電池の昇温装置。
An air-cooled fuel that heats a fuel cell having a heat medium passage that is isolated from an electrolyte and is supplied with a heat medium independent of a reaction gas, by supplying a heat medium to the heat medium passage through a supply pipe having a blower. In the battery temperature raising device, a starting burner that supplies the heat medium to the supply pipe line on the blower suction side;
1. A temperature raising device for an air-cooled fuel cell, comprising an air supply means for mixing air with a heat medium from the burner.
JP62133006A 1987-05-28 1987-05-28 Temperature rising device for air cooled fuel cell Pending JPS63298975A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62133006A JPS63298975A (en) 1987-05-28 1987-05-28 Temperature rising device for air cooled fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62133006A JPS63298975A (en) 1987-05-28 1987-05-28 Temperature rising device for air cooled fuel cell

Publications (1)

Publication Number Publication Date
JPS63298975A true JPS63298975A (en) 1988-12-06

Family

ID=15094581

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62133006A Pending JPS63298975A (en) 1987-05-28 1987-05-28 Temperature rising device for air cooled fuel cell

Country Status (1)

Country Link
JP (1) JPS63298975A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6266578A (en) * 1985-09-19 1987-03-26 Fuji Electric Co Ltd Air cooling type fuel cell power generating system
JPS6280968A (en) * 1985-10-03 1987-04-14 Hitachi Ltd Fuel cell power generating plant

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6266578A (en) * 1985-09-19 1987-03-26 Fuji Electric Co Ltd Air cooling type fuel cell power generating system
JPS6280968A (en) * 1985-10-03 1987-04-14 Hitachi Ltd Fuel cell power generating plant

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