JPS6210874A - Liquid fuel cell - Google Patents
Liquid fuel cellInfo
- Publication number
- JPS6210874A JPS6210874A JP60148309A JP14830985A JPS6210874A JP S6210874 A JPS6210874 A JP S6210874A JP 60148309 A JP60148309 A JP 60148309A JP 14830985 A JP14830985 A JP 14830985A JP S6210874 A JPS6210874 A JP S6210874A
- Authority
- JP
- Japan
- Prior art keywords
- methanol
- electrode
- chamber
- fuel electrode
- air electrode
- 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
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04186—Arrangements for control of reactant parameters, e.g. pressure or concentration of liquid-charged or electrolyte-charged reactants
-
- 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は簡潔な構成で間欠使用時の電池温度の暴走を防
止した液体燃料電池に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a liquid fuel cell that has a simple structure and prevents runaway cell temperature during intermittent use.
(従来技術)
従来より燃料電池は知られているが、最近メタノールな
どを燃料として用いる液体燃料電池が自動車の電源とし
て従来のバッテリに代りまたはバッテリと併用すること
が考えられている。(Prior Art) Fuel cells have been known for a long time, but recently it has been considered that liquid fuel cells using methanol or the like as a fuel can be used instead of or in combination with conventional batteries as a power source for automobiles.
液体燃料電池は、電解液を入れた電槽内に燃料極と空気
極(M累積ともいう)とを隔膜を隔てて配置してあり、
下記の電気化学反応により起電力を取り出している。A liquid fuel cell has a fuel electrode and an air electrode (also called M cumulative) placed in a battery containing an electrolyte with a diaphragm separating them.
Electromotive force is extracted by the electrochemical reaction described below.
燃料極: CH30H+lI20 →Co2+6H+6
e空気極:3/2 o2+6H+6e →3■20
この液体燃料電池を小型電源として車両に使用する場合
について考えてみると、車両は運転しないときもあるの
で、この間液体燃料電池は使用されない。しかし、液体
燃料電池をこのように間欠使用した場合、以下の問題が
生じる。Fuel electrode: CH30H+lI20 →Co2+6H+6
e Air electrode: 3/2 o2+6H+6e →3■20
If we consider the case where this liquid fuel cell is used as a small power source in a vehicle, there are times when the vehicle is not being driven, so the liquid fuel cell is not used during this period. However, when a liquid fuel cell is used intermittently in this way, the following problems occur.
すなわち、間欠使用時の休止期間においては隔膜上の微
小なピンホールを通して燃料極液室から空気極液室へメ
タノールが多少拡散透過する。この休止期間が数日以上
となるとメタノールの濃度拡散は平衡状態となり両室と
も同濃度に達する。That is, during the rest period during intermittent use, some methanol diffuses and permeates from the anode fluid chamber to the air cathode fluid chamber through minute pinholes on the diaphragm. If this pause period is longer than several days, the concentration diffusion of methanol will reach an equilibrium state and the same concentration will be reached in both chambers.
この様な状態において、電池に空気を供給し起動状態と
すると、空気極上で空気極液室にあるメタノールは拡散
供給された空気により急速に触媒燃焼(CH30H+3
./20.→CO2+2H20〉する。この燃焼は上述
した電気化学反応と異なり熱化学反応であり、発熱を伴
なうため電池温度は上昇する。In such a state, when air is supplied to the battery and the battery is activated, the methanol in the air cathode liquid chamber on the air electrode rapidly undergoes catalytic combustion (CH30H+3
.. /20. →CO2+2H20〉. Unlike the electrochemical reaction described above, this combustion is a thermochemical reaction and is accompanied by heat generation, which increases the battery temperature.
一方、電池温度の上昇に伴ないメタノールの拡散透過速
度も増大し、これによってメタノールの空気極液室への
拡散が促進され空気極上の触媒燃焼が加速される。この
悪循環により電池温度は暴走し、メタノール燃料の電気
エネルギーへの変換効率は次第に低下する。On the other hand, as the battery temperature rises, the diffusion permeation rate of methanol also increases, which promotes the diffusion of methanol into the air cathode chamber and accelerates catalytic combustion on the air electrode. This vicious cycle causes the battery temperature to run out of control, and the efficiency of converting methanol fuel into electrical energy gradually decreases.
この問題を解決するための液体燃料電池の温度制御方式
としていくつか提案されている(実開昭59−1155
74および実開昭59−117067)。To solve this problem, several temperature control methods for liquid fuel cells have been proposed (Utility Model Application No. 59-1155).
74 and Utility Model Publication No. 59-117067).
これらの制御方式は電解液を外部循環させて放熱しその
温度を低下させるか、あるいは空気極側に設けたブロア
ーによって空気極に空気を送り込んで冷却し電解液温度
を低下させるものである。These control methods either circulate the electrolyte externally to radiate heat and lower its temperature, or use a blower installed on the air electrode to blow air into the air electrode to cool it and lower the temperature of the electrolyte.
しかしながら、このような従来の温度制御方式にあって
は、ポンプヤブロアーなどの補機を用いるためシステム
が大型化あるいは複雑化し、そのため燃料電池により発
生した電気エネルギーが補機によって消費される割合が
大きく、燃料の利用効率が低いという問題点があった。However, in such conventional temperature control methods, the system becomes larger or more complex due to the use of auxiliary equipment such as pumps and blowers, and as a result, the proportion of electrical energy generated by the fuel cell consumed by the auxiliary equipment is reduced. The problem was that the efficiency of fuel use was low.
(発明の目的および構成)
本発明は上記の点にかんがみてなされたもので、間欠使
用時における液体電池の温度暴走を簡潔な構成で防止す
ることを目的とし、そのため空気極液室内に補助燃料極
を設け、起動時に該補助燃料極を作動させて空気極液室
のメタノールを消費し、その濃度を低下させ、空気極上
のメタノールの触媒燃焼を抑制し、その後は主燃料極を
作動させるように構成した。(Purpose and Structure of the Invention) The present invention has been made in view of the above points, and an object of the present invention is to prevent temperature runaway of a liquid battery during intermittent use with a simple structure. At startup, the auxiliary fuel electrode is activated to consume methanol in the air electrode liquid chamber, reduce its concentration, and suppress the catalytic combustion of methanol on the air electrode, and then the main fuel electrode is activated. It was configured as follows.
(実施例) 以下、本発明を図面に基づいて説明する。(Example) Hereinafter, the present invention will be explained based on the drawings.
第1図は本発明による液体燃料電池の一実施例の概略線
図であり、1は主燃料極、2は補助燃料極、3は空気極
、4は隔膜、5は燃料電池の電槽、6は燃料極液室、7
は空気極液室である。空気極液室7には希硫酸(10〜
30wt%)が、燃料極液室6には希硫酸(10〜30
wt%)とメタノール(5〜20wt%)との混合溶液
が入っている。FIG. 1 is a schematic diagram of an embodiment of a liquid fuel cell according to the present invention, in which 1 is a main fuel electrode, 2 is an auxiliary fuel electrode, 3 is an air electrode, 4 is a diaphragm, 5 is a fuel cell container, 6 is the fuel electrode liquid chamber, 7
is the catholyte chamber. Dilute sulfuric acid (10~
30wt%), but the fuel electrode liquid chamber 6 contains dilute sulfuric acid (10~30wt%).
Contains a mixed solution of (wt%) and methanol (5 to 20 wt%).
しかし、間欠使用の際、数日以上放置すると燃料極液室
6内のメタノールが濃度拡散し、燃料極液室6および空
気極液室7においてメタノールが拡散平衡状態となる。However, during intermittent use, if left for several days or more, methanol in the fuel electrode chamber 6 will be concentrated and diffused, and methanol will be in a diffusion equilibrium state in the fuel electrode chamber 6 and the air electrode chamber 7.
8は補助メタノール極2と空気極3との接触を防止する
ためのプラスチック性フィルタであり、9は燃料として
のメタノールの取入口である。11は主燃料極1および
補助燃料極2にそれぞれ接続される接点11a、11b
を切換える切換スイッチであり、10は主燃料極1また
は補助燃料極2と空気極3との間の起電力を検出しその
出力に応じて切換スイッチ11を切換制御するコントロ
ーラである。8 is a plastic filter for preventing contact between the auxiliary methanol electrode 2 and the air electrode 3, and 9 is an inlet for methanol as fuel. 11 are contacts 11a and 11b connected to the main fuel electrode 1 and the auxiliary fuel electrode 2, respectively.
10 is a controller that detects the electromotive force between the main fuel electrode 1 or the auxiliary fuel electrode 2 and the air electrode 3 and controls the changeover switch 11 according to the output thereof.
以上のように構成すると、電池を負荷に接続しスタート
スイッチ(図に示していない)を入れるとくスタートコ
マンドが出力する)、切換スイッチ11は接点11bに
接続され、補助燃料極2において下記の化学反応が起こ
る。With the above configuration, when the battery is connected to the load and the start switch (not shown) is turned on, a start command is output.) The changeover switch 11 is connected to the contact 11b, and the following chemical A reaction occurs.
CH30H+H20→CO2+6H+6e−この化学反
応により空気極液室7内のメタノールは急速に消費され
、メタノール濃度が低下する。CH30H+H20→CO2+6H+6e- Due to this chemical reaction, the methanol in the air catholyte chamber 7 is rapidly consumed, and the methanol concentration decreases.
この結果、空気極3上でのメタノールの触媒燃焼は抑制
され温度暴走が防止される。As a result, catalytic combustion of methanol on the air electrode 3 is suppressed and temperature runaway is prevented.
次に補助燃料極2と空気極3との間の出力電圧は空気極
液室7内のメタノール濃度の低下によって急速に低下す
るが、この電圧低下率がスタート時の80〜90%とな
ったときコントローラ10からの指令により切換スイッ
チ11は接点11bから接点11aに切り換えられ、そ
れ以後は主燃料極1が用いられる。Next, the output voltage between the auxiliary fuel electrode 2 and the air electrode 3 rapidly decreased due to the decrease in the methanol concentration in the air electrode liquid chamber 7, and this voltage drop rate was 80 to 90% of the starting voltage. At this time, the changeover switch 11 is switched from the contact 11b to the contact 11a by a command from the controller 10, and from then on, the main fuel electrode 1 is used.
なお上記実施例においては電圧低下率を基準にして補助
燃料極から主燃料極への切換を行なったが、起動から一
定時間経過後自動的に切換えるようにしてもよい。また
切換はコントローラによらず手動で行なってもよい。In the above embodiment, switching from the auxiliary fuel electrode to the main fuel electrode was performed based on the voltage drop rate, but the switching may be performed automatically after a certain period of time has passed since startup. Further, the switching may be performed manually without using the controller.
(発明の効果)
以上説明してきたように、本発明においては、空気極液
室に設けた補助燃料極を用いて電池を起動させ、これに
よって空気極液室のメタノールを消費しその濃度を急速
に低下させるように構成したため、燃料電池を間欠使用
する際の電池起動時における空気極上のメタノールの触
媒燃焼による温度暴走をポンプやブロアーのような補機
を必要としない簡潔な構成で防止できるという効果が得
られる。(Effects of the Invention) As explained above, in the present invention, the auxiliary fuel electrode provided in the catholyte chamber is used to start the battery, thereby consuming methanol in the catholyte chamber and rapidly increasing its concentration. This makes it possible to prevent temperature runaway due to catalytic combustion of methanol on the air electrode when the fuel cell is started up during intermittent use, with a simple configuration that does not require auxiliary equipment such as pumps or blowers. Effects can be obtained.
第1図は本発明による液体燃料電池の構造を示す概略線
図である。FIG. 1 is a schematic diagram showing the structure of a liquid fuel cell according to the present invention.
Claims (1)
と補助燃料極とを設け、起動時には前記補助燃料極を作
動させその後は切換手段を用いて前記主燃料極を作動さ
せるように構成したことを特徴とする液体燃料電池。A main fuel electrode is provided in the fuel electrode liquid chamber, and an air electrode and an auxiliary fuel electrode are provided in the air cathode liquid chamber, and the auxiliary fuel electrode is operated at startup, and thereafter the main fuel electrode is operated using a switching means. A liquid fuel cell characterized by comprising:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60148309A JPS6210874A (en) | 1985-07-08 | 1985-07-08 | Liquid fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60148309A JPS6210874A (en) | 1985-07-08 | 1985-07-08 | Liquid fuel cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6210874A true JPS6210874A (en) | 1987-01-19 |
Family
ID=15449904
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60148309A Pending JPS6210874A (en) | 1985-07-08 | 1985-07-08 | Liquid fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6210874A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6099788A (en) * | 1983-11-02 | 1985-06-03 | 株式会社シマノ | Derailer for bicycle |
| US5380253A (en) * | 1992-03-23 | 1995-01-10 | Maeda Industries, Ltd. | Bicycle rear derailleur |
| US5397273A (en) * | 1993-02-03 | 1995-03-14 | Shimano Inc. | Rear derailleur for a bicycle |
| US5421786A (en) * | 1993-02-03 | 1995-06-06 | Shimano Inc. | Rear derailleur bracket |
-
1985
- 1985-07-08 JP JP60148309A patent/JPS6210874A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6099788A (en) * | 1983-11-02 | 1985-06-03 | 株式会社シマノ | Derailer for bicycle |
| US5380253A (en) * | 1992-03-23 | 1995-01-10 | Maeda Industries, Ltd. | Bicycle rear derailleur |
| US5397273A (en) * | 1993-02-03 | 1995-03-14 | Shimano Inc. | Rear derailleur for a bicycle |
| US5421786A (en) * | 1993-02-03 | 1995-06-06 | Shimano Inc. | Rear derailleur bracket |
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