JPS60200470A - portable fuel cell - Google Patents
portable fuel cellInfo
- Publication number
- JPS60200470A JPS60200470A JP59055704A JP5570484A JPS60200470A JP S60200470 A JPS60200470 A JP S60200470A JP 59055704 A JP59055704 A JP 59055704A JP 5570484 A JP5570484 A JP 5570484A JP S60200470 A JPS60200470 A JP S60200470A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- chamber
- electrode
- fuel cell
- oxidizer
- 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
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0662—Treatment of gaseous reactants or gaseous residues, e.g. cleaning
-
- 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
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
-
- 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
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04119—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
- H01M8/04156—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying with product water removal
-
- 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
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 〔発明の利用分野〕 本発明はポータプルタイプの燃料霜;池に係り。[Detailed description of the invention] [Field of application of the invention] The present invention relates to a portaple type fuel frost pond.
特に電極反応によって発生する生成物を系外に排出する
ことなく稼動できる燃料電池に関する。In particular, the present invention relates to a fuel cell that can be operated without discharging products generated by electrode reactions to the outside of the system.
近年、家電品や産業用機器のコンバク]・化、コードレ
ス化に伴い新しい小型軽重な可搬電源の開発が待望され
ている。これに応える電源のひとつとして、ポータプル
な燃料電池がφげられる。燃料電池は燃料と酸化剤であ
る空気中の酸素との化学反応を直接電気エネルギーに変
換させる装置である。そのため、騒音が少ない、充電の
わずられしさが無い等の他の可搬電源に比較して利点が
多い。In recent years, as home appliances and industrial equipment become more compact and cordless, the development of new compact, lightweight, and portable power sources has been eagerly awaited. Portable fuel cells are one of the power sources that can meet this demand. A fuel cell is a device that directly converts the chemical reaction between fuel and oxygen in the air, which is an oxidant, into electrical energy. Therefore, it has many advantages compared to other portable power sources, such as less noise and no hassle of charging.
燃料電池を小型電源として利用する場合、種々の問題が
生じるが、そのひとつとして電極反応により発生したN
20.CO2、N2 などの反応生成物が電池系外に排
出され、これに伴って燃料又は電解液が1を池系外に放
出される問題がある。このため、燃料電池を電源として
搭載1〜だ機器ヤその周辺の機器等において′観池系内
からの排出物が付着し、酸化腐食の原因となり、また排
出物が人体に悪影響を及ぼすおそれがある。When using fuel cells as a small power source, various problems arise, one of which is the N generated by electrode reactions.
20. There is a problem in that reaction products such as CO2 and N2 are discharged outside the battery system, and along with this, fuel or electrolyte 1 is discharged outside the pond system. For this reason, there is a risk that emissions from the pond system will adhere to equipment that uses fuel cells as a power source and surrounding equipment, causing oxidation and corrosion, and that the emissions may have an adverse effect on the human body. be.
本発明の目的は、燃料電池稼動による反応生成物を電池
系外部に放出することなく、燃料電池の本体内で処理で
きるポータプル型燃料電池を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a portable fuel cell that can process reaction products generated during fuel cell operation within the main body of the fuel cell without releasing them to the outside of the cell system.
本発明は、電池糸内部に燃料′iイ池イwK動による反
応生成物を収納する手段、捷たは反応生成物を吸収する
手段を設け、反応生成物が電池系外に排出しないように
したものである。The present invention provides a means for storing reaction products caused by fuel movement, a means for cutting or absorbing reaction products inside the battery thread, and prevents the reaction products from being discharged outside the battery system. This is what I did.
すなわち、本発明において電極反応生成(吻は電池系内
部において処理される。処理手段としては。That is, in the present invention, the electrode reaction generation (the proboscis is processed inside the battery system. As a processing means.
生成物質を選択的に吸収する吸収剤を電池系内部に設置
する手段、生成物質を電池糸夕1部に漏らすことなく電
池系内部に溜めるだめのタンク等の手段がある。There are means such as installing an absorbent inside the battery system that selectively absorbs the generated substances, and a tank that stores the generated substances inside the battery system without leaking them into the battery cell.
反応生成物のうちCO2ガスの処理に関しては。Regarding the treatment of CO2 gas among the reaction products.
Co2吸収剤を用いる。CO2吸収剤としては、CO2
ガスを選択的に吸収、保持し得るものであれば特に限定
はない。例えば、ノーダライム、苛性アルカリ、エタノ
ールアミンなどがあげられる。Use Co2 absorbent. As a CO2 absorbent, CO2
There is no particular limitation as long as it can selectively absorb and retain gas. Examples include nodalime, caustic alkali, and ethanolamine.
これらのうち本発明においては特に、水酸化カルシウム
などの固体状のものが取扱いと002吸収能の点からみ
て好ましい、、CO2吸収剤は、燃料室、又は燃料供給
タンク内に設置する。その時、C02吸収剤が液体燃料
と混合するのを防止するだめ、液体、固体の通過を阻止
し、気体のみ通す分離膜によって、隔離する必要がある
。気体と固液を分離するのに用いる分離膜としては、フ
ッ素系樹脂の多孔質膜などの撥水性を有し、ガス透過性
のものならば特に限定はされない。膜i−構成する材料
としては、ポリテトラフルオロエチレン。Among these, in the present invention, a solid CO2 absorbent such as calcium hydroxide is particularly preferred from the viewpoint of handling and 002 absorption capacity.The CO2 absorbent is installed in the fuel chamber or fuel supply tank. At that time, in order to prevent the CO2 absorbent from mixing with the liquid fuel, it is necessary to isolate it with a separation membrane that blocks the passage of liquids and solids and allows only gas to pass. The separation membrane used to separate gas and solid-liquid is not particularly limited as long as it is water repellent and gas permeable, such as a porous fluororesin membrane. Membrane i - The constituent material is polytetrafluoroethylene.
ポリクロロトリフルオロエチレンなどヤこ11.らを含
む重合体などがある。これらの材料を多孔質なフィルム
としたものを用いることができる。Polychlorotrifluoroethylene, etc. 11. There are polymers containing these. Porous films made of these materials can be used.
CO2吸収剤は、電池本体と着脱可能な容器あるいは1
着脱可能な燃料供給タンクの一部に置き。The CO2 absorber is placed in a container or container that is detachable from the battery body.
Placed in part of the removable fuel supply tank.
電池稼動によってCO2吸収剤の002吸収能が低下し
た場合、電池本体から容器ごとあるいは。If the 002 absorption capacity of the CO2 absorbent decreases due to battery operation, remove the entire container from the battery body or the like.
吸収剤のみを新しいものと交換する。Replace only the absorbent with a new one.
生成水の吸水剤には、高分子電解質架橋繊維等のような
吸水力及び保水力の大きなものなら特に限定しないが吸
水率50〜1o00 (g/g )が望ましい。材料と
しては例えば、デンプン−アクリロニトリル加水分解物
、セルロースグラフト化物。The water-absorbing agent for produced water is not particularly limited as long as it has a high water-absorbing power and water-holding power, such as crosslinked polymer electrolyte fibers, but it is desirable that the water absorbing rate is 50 to 1000 (g/g). Examples of the material include starch-acrylonitrile hydrolyzate and cellulose grafted product.
ポリアクリル酸ナトリウム、ポリビニルアルコール架橋
物などがある。これら高吸水性樹脂の微粉末(平均粒子
径(1,05〜0.1 rtan )をそのまま用いる
か、又は、パルプに挾む又は基材にコーディングするな
どシート状に加工したもの、繊維状のものなどを用いる
。高吸収性樹脂は吸水状態においてはゲル化し膨潤する
ので、微粉末状のものよりシート状又は繊維状のものが
使いやすい。Examples include sodium polyacrylate and crosslinked polyvinyl alcohol. Fine powder of these super absorbent resins (average particle size (1.05 to 0.1 rtan) can be used as is, or processed into a sheet form such as sandwiched between pulps or coated on a base material, or fibrous Since the superabsorbent resin gels and swells when it absorbs water, it is easier to use a sheet or fibrous resin than a fine powder.
吸水剤は、空気室出口燃料供給タンクの一部に保持し、
着脱可能な容器内に設置することができる。吸水能力が
低下した場合には、吸水剤を有する容器ごと燃料電池本
体からはずすか又は吸水剤のみを新品と取り替える。The water absorbing agent is held in a part of the air chamber outlet fuel supply tank,
It can be installed in a removable container. If the water absorption capacity decreases, either remove the entire container containing the water absorbent from the fuel cell body, or replace only the water absorbent with a new one.
一方、生成凝縮水の電池系外への排出の防止には、吸水
剤を使用しなくとも燃料電池本体の一部に生成水溜めタ
ンクを設置する方法もある。タンクは電池本体と着脱可
能なものとし、生成水タンクとして独立しているかある
いは、燃料供給タンクの一部全生成水タンクとしたもの
である。生成水タンクに溜まった水は、電池の運転休止
の際。On the other hand, in order to prevent the generated condensed water from being discharged outside the cell system, there is also a method of installing a generated water storage tank in a part of the fuel cell body without using a water absorbing agent. The tank is removable from the battery main body, and is either an independent generated water tank, or a part of the fuel supply tank is a generated water tank. The water that collects in the generated water tank is removed when the battery is out of operation.
電池系外にまとめて滲棄する。Discard all of it outside the battery system.
第1図は本発明の一実施例を示し、電池スタック1に電
池枠2が組込まれ、電池スタック1内の燃料室に燃料を
供給するだめの燃料タンク3が取シ外し自在に設けられ
ている。電池スタック1内の空気極に連通してカートリ
ッジ式の生成水タンク4が取シ付けられ、燃料極に連通
して炭酸ガス出口5が設けられている。図中、6は空気
出口であって空気極で利用されない余剰の空気が排出さ
れるようになっておυ、この空気出口6に撥水性多孔質
が張設されているUまた生成水タンク40入口には特に
図示していないが′電池転倒などによる生成水タンクか
ら電池本体への水の逆流を防ぐだめの逆流防止弁が介設
されている。FIG. 1 shows an embodiment of the present invention, in which a battery frame 2 is assembled into a battery stack 1, and a fuel tank 3 for supplying fuel to a fuel chamber in the battery stack 1 is removably provided. There is. A cartridge-type generated water tank 4 is attached in communication with the air electrode in the battery stack 1, and a carbon dioxide gas outlet 5 is provided in communication with the fuel electrode. In the figure, reference numeral 6 denotes an air outlet through which excess air not used in the air electrode is discharged, and this air outlet 6 is lined with a water-repellent porous material. Also, a produced water tank 40 Although not particularly shown in the drawings, a backflow prevention valve is provided at the inlet to prevent backflow of water from the produced water tank to the battery body due to the battery falling over.
第2図は本発明の他の実施例を示し、第1図に示す実施
例と異なる点は生成水タンク4の内に不織布の間に電解
質架橋繊維7を挾んだシートを詰めていることである。FIG. 2 shows another embodiment of the present invention, which differs from the embodiment shown in FIG. 1 in that a sheet in which electrolyte crosslinked fibers 7 are sandwiched between nonwoven fabrics is packed in the produced water tank 4. It is.
しだがって他の構成部材は第1図と同一符号で示してい
る。Other components are therefore designated by the same reference numerals as in FIG.
第3図は本発明の更に他の実施例を示し、カートリッジ
式の使いすて方式とした燃料タンク3内を3つに区画し
、上部に燃料極に連通ずる炭酸ガス出口に取シ外し自在
の入口を有する炭酸ガス吸収剤収納室8を設け、下部に
空気極に連通ずる空気出口に取り外し自在の入口を有す
る生成水タンク9を設け、タンクの中段部が燃料を収納
する区画となっている。Fig. 3 shows still another embodiment of the present invention, in which the interior of the fuel tank 3 is a cartridge type disposable type, and is divided into three parts, and a carbon dioxide gas outlet communicating with the fuel electrode is provided at the upper part, and the fuel tank 3 is removable. A carbon dioxide absorbent storage chamber 8 having an inlet is provided, and a generated water tank 9 having a removable inlet and an air outlet communicating with the air electrode is provided at the bottom, and the middle part of the tank serves as a compartment for storing fuel. There is.
なお1本発明はメタノール空気燃料電池の他にアルカリ
電解液型ヒドラジン−空気燃料電池、水素−酸素燃料電
池にも適用できるが、ボータプル型の面からはメタノー
ル−を気燃料電池に最も有効である。In addition to methanol-air fuel cells, the present invention can also be applied to alkaline electrolyte type hydrazine-air fuel cells and hydrogen-oxygen fuel cells, but from the viewpoint of the vortaple type, methanol-air fuel cells are most effective. .
試験例1
第1図に示す燃料電池において、η1. MILI2O
3きさを150 X 1.50 X 180 (cnl
)とし、生成水タンクの容積を500 cc (@池本
体の体積の約10チである)とし、筐た撥水性多孔質膜
としてGOfLE−TEX(@工社製)のフィルム(空
気流量2000〜3000 cc / mtn/=<
)を用いた。Test Example 1 In the fuel cell shown in FIG. 1, η1. MILI2O
3 size 150 x 1.50 x 180 (cnl
), the volume of the produced water tank was set to 500 cc (approximately 10 cm of the volume of the pond body), and the water-repellent porous membrane encased was a GOofLE-TEX (manufactured by Kosha) film (with an air flow rate of 2000~ 3000 cc/mtn/=<
) was used.
本電池を定格出力50Wで稼動させた。This battery was operated at a rated output of 50W.
稼動中空気室出口から()ORE −T E Xのフィ
ルムを通して空気のみが排出され、生成水は凝縮して生
成水タンク中へ流れることが確認できた。空気室出口あ
るいは電池枠からの生成水の流出は全くなかった。この
ように生成水凝縮タンクを設けることにニジカソード反
応により生成した水を電池系外に排出することなく、取
扱いが容易で安全性の高い燃料電池となる。During operation, it was confirmed that only air was discharged from the outlet of the air chamber through the ()ORE-TEX film, and that the produced water condensed and flowed into the produced water tank. There was no outflow of produced water from the air chamber outlet or the battery frame. By providing the produced water condensation tank in this manner, the water produced by the rainbow cathode reaction is not discharged outside the cell system, resulting in a fuel cell that is easy to handle and highly safe.
試験例2
第2図に示す燃料電池において、電解質架橋繊維として
、スミカゲルS−5O(ビニルアルコール/アクリル酸
共重合体)を用いた。電池は試験Q1
例1と同じ出力50Wである。電池を憚扉ノさせると、
生成水はタンクへ流れ込み、中の吸水シーI・に吸収さ
れた。Test Example 2 In the fuel cell shown in FIG. 2, Sumikagel S-5O (vinyl alcohol/acrylic acid copolymer) was used as the electrolyte crosslinked fiber. The battery has the same output of 50W as Test Q1 Example 1. If you leave the battery in the door,
The produced water flowed into the tank and was absorbed into the water absorbing sea I.
スミカゲル5−50の吸収率は450 g / gであ
り、0.5g用いたため、8時間市、池稼動では生成水
はすべて吸収されヒドロゲル化してタンク内に保持され
た。電池の周辺に生成水の流出けなかった。The absorption rate of Sumikagel 5-50 was 450 g/g, and since 0.5 g was used, all the produced water was absorbed during the 8-hour operation, turned into a hydrogel, and was retained in the tank. The generated water could not flow around the battery.
試験例3
第3図に示す燃料電池において、炭酸ガス吸収剤収納室
8に水酸化カルシウムのペレット(粒径1〜2■)を充
填し、生成水タンク9にスミカゲル5−50を収納した
。Test Example 3 In the fuel cell shown in FIG. 3, calcium hydroxide pellets (particle size 1 to 2 square meters) were filled in the carbon dioxide absorbent storage chamber 8, and Sumikagel 5-50 was stored in the produced water tank 9.
燃料電池のガス排水口付近の炭酸ガス濃度を測定した結
果、0.04%であった。因みに炭1Wガス吸収剤収納
室8を通過させることなく、そのまま排出されるカス中
のCOz濃度は98.7 %であった。The carbon dioxide concentration near the gas drain port of the fuel cell was measured and found to be 0.04%. Incidentally, the COz concentration in the waste that was discharged as it was without passing through the charcoal 1W gas absorbent storage chamber 8 was 98.7%.
空気中の炭酸ガス濃度は一般に1)03〜0.04チで
ある。上記の結果1反応生成CC)gガスはは(10)
ぼ100%吸収剤に吸収されたことがわかった。The carbon dioxide concentration in the air is generally 1)03 to 0.04. As a result of the above, it was found that almost 100% of the CC)g gas produced by reaction 1 was absorbed by the absorbent.
また、生成水は電池系外に、全く洩れ出なかった。Furthermore, no generated water leaked out of the battery system.
本発明によれば、小型電源として用いるボータプル燃料
電池において、電池稼動時、電極反応による生成物は発
電装置内に収納されるため、電池系外への反応生成物の
排出が無くなる。従って、反応生成物の排出に同伴する
と考えられる酸あるいはアルカリの電解液ミストの電池
糸外への放出が避けられる。また、炭酸ガスは水に浴け
ると酸性となり、腐食の原因となっていたが、これも電
池系内にて処理することが可能になりざらに生成水を電
池系外に出さないことにより、小型電源としての通用範
囲が広がる。According to the present invention, in a vortaple fuel cell used as a small power source, products resulting from electrode reactions are stored within the power generation device during operation of the cell, so that reaction products are not discharged outside the cell system. Therefore, the release of acid or alkaline electrolyte mist, which is considered to accompany the discharge of reaction products, to the outside of the battery thread can be avoided. In addition, when carbon dioxide gas is exposed to water, it becomes acidic and causes corrosion, but now it is now possible to process this within the battery system, and by not letting the generated water out of the battery system, The range of applications as a small power source is expanded.
第1図、第2図および第3図はそれぞれ本発明の実施例
を示すボータプル型メタノール−燃料電池の概略断面図
である。
1・・・電池スタッフ、2・・・電池枠、3・・・燃料
タンク。
(11)
4.9・・・生成水タンク、5・・・炭酸ガス出口、6
・・・空気出口、7・・・電解質架橋繊維(吸水剤)、
8・・・炭酸カス吸収剤収納室。
代理人 弁理士 鵜沼辰之
(12)
茅l口
茅2 図
第1頁の続き
■発明者 州名 秀治部 日立市幸町
所内
0発 明 者 堀 場 達 雄 日立市幸町所内
0発 明 者 熊 谷 輝 雄 日立市幸町所内
0発 明 者 1)村 弘 毅 日立市幸町所内FIGS. 1, 2, and 3 are schematic sectional views of a vortaple methanol fuel cell showing an embodiment of the present invention, respectively. 1...Battery staff, 2...Battery frame, 3...Fuel tank. (11) 4.9... Produced water tank, 5... Carbon dioxide gas outlet, 6
... Air outlet, 7... Electrolyte crosslinked fiber (water absorbing agent),
8... Carbon dioxide absorbent storage chamber. Agent Patent attorney Tatsuyuki Unuma (12) Kaya Kuchi 2 Figure continued from page 1 Inventor State Hidejibu Hitachi City Saiwai-cho site 0 authors Horiba Tatsuo Hitachi City Saiwai-cho site 0 authors Kuma Teruo Tani Inside Saiwai-cho, Hitachi City0 Inventor 1) Takeshi Mura Inside Saiwai-cho, Hitachi City
Claims (1)
剤極側に酸化剤室を設け、燃料極側に燃料室を設けた単
電池を1細板上積層させたポータプル型燃料電池におい
て、前記酸化剤室から燃料電池内のガス出口に至るまで
の通路と連通ずる個所に電極反応によって生成する水を
収納するタンクを設けたことを特徴とするポータプル型
燃料電池。 2、特許請求の範囲第1項において、前記タンク中に高
分子架橋生成物を収納したことを特徴とするボータプル
型燃料電池9゜ 3、特許請求の範囲第1項において、前記タンクが、電
池本体に着脱自在に設けられていることを特徴とするポ
ータプル型燃料電池。 4、酸化剤極と燃料極との間に電解質室を有し、酸化剤
極側に酸化剤室を設け、燃料極側に燃料室を設けた単電
池を1細板上積層させたポータプル型燃料電池において
、前記燃料極から燃料電池内のガス排出口に至るまでの
通路と連通ずる個所に′l!lic極反応生成物を選択
的に吸収する吸収剤を収納したタンクを設けたことを特
徴とするボータプル型燃料電池。 5、特許請求の範囲第4項において、前記蜜、極反応生
成物が炭酸ガスであることを%徴とするポータプル型燃
料電池。 6、酸化剤室と燃料極との間に電解質室を有17゜酸化
剤極側に酸化剤室を設け、燃料極側に燃料室を設けた単
電池を1細板上積層させたボータプル型燃料醒池におい
て、前記酸化剤室から燃料電池のガス出口に至るまでの
通路と連通ずる個所に電極反応によって生成する水を収
納する室と、前記燃料極から燃料電池内のガス排出口に
至るまでの通路と連通する個所に電極反応生成物を選択
的に吸収する吸収剤を収納する室とを燃料タンクと一体
に設けたことを特徴とするボータプル型燃料電池。[Scope of Claims] 1. A unit cell having an electrolyte chamber between an oxidizer electrode and a fuel electrode, an oxidizer chamber provided on the oxidizer electrode side, and a fuel chamber provided on the fuel electrode side is formed into one thin plate. A portaple fuel cell stacked above, characterized in that a tank for storing water produced by an electrode reaction is provided at a location communicating with a passage from the oxidizer chamber to a gas outlet in the fuel cell. type fuel cell. 2. Claim 1, wherein the tank contains a cross-linked polymer product. 2. Claim 1, wherein the tank contains a polymer crosslinked product. A portable fuel cell is characterized by being detachably installed in the main body. 4. A portapull type cell that has an electrolyte chamber between the oxidizer electrode and the fuel electrode, an oxidizer chamber on the oxidizer electrode side, and a fuel chamber on the fuel electrode side, stacked on one thin plate. In the fuel cell, there is a 'l! 1. A both-pull fuel cell characterized by being provided with a tank containing an absorbent that selectively absorbs LIC electrode reaction products. 5. The portaple fuel cell according to claim 4, wherein the polar reaction product is carbon dioxide. 6. An electrolyte chamber is provided between the oxidizer chamber and the fuel electrode.17゜Botaple type in which single cells with an oxidizer chamber provided on the oxidizer electrode side and a fuel chamber provided on the fuel electrode side are stacked on one thin plate. In the fuel purification pond, there is a chamber for storing water generated by the electrode reaction in a place communicating with a passage from the oxidizer chamber to the gas outlet of the fuel cell, and a chamber for storing water generated by the electrode reaction from the fuel electrode to the gas outlet in the fuel cell. 1. A both-pull type fuel cell characterized in that a chamber for housing an absorbent that selectively absorbs electrode reaction products is provided integrally with a fuel tank at a location communicating with a passageway between the electrodes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59055704A JPS60200470A (en) | 1984-03-23 | 1984-03-23 | portable fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59055704A JPS60200470A (en) | 1984-03-23 | 1984-03-23 | portable fuel cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS60200470A true JPS60200470A (en) | 1985-10-09 |
Family
ID=13006271
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59055704A Pending JPS60200470A (en) | 1984-03-23 | 1984-03-23 | portable fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60200470A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0482222A1 (en) * | 1990-10-20 | 1992-04-29 | Asea Brown Boveri Ag | Method for the separation of nitrogen and carbon dioxide and concentration of the latter in energysupplying oxydation- and combustion processes |
| JPH0676852A (en) * | 1992-08-31 | 1994-03-18 | Sanyo Electric Co Ltd | Portable power source |
| US5364711A (en) * | 1992-04-01 | 1994-11-15 | Kabushiki Kaisha Toshiba | Fuel cell |
| JP2003036879A (en) * | 2001-07-19 | 2003-02-07 | Casio Comput Co Ltd | Power system |
| WO2004004049A1 (en) * | 2002-06-28 | 2004-01-08 | Nec Corporation | Fuel cell and method of use teereof |
| US6777118B2 (en) * | 2001-01-24 | 2004-08-17 | Casio Computer Co., Ltd. | Power supply system, fuel pack constituting the system, and device driven by power generator and power supply system |
| JP2010108938A (en) * | 2009-11-06 | 2010-05-13 | Casio Computer Co Ltd | Fuel container |
| JP2010114083A (en) * | 2009-11-06 | 2010-05-20 | Casio Computer Co Ltd | Fuel container |
-
1984
- 1984-03-23 JP JP59055704A patent/JPS60200470A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0482222A1 (en) * | 1990-10-20 | 1992-04-29 | Asea Brown Boveri Ag | Method for the separation of nitrogen and carbon dioxide and concentration of the latter in energysupplying oxydation- and combustion processes |
| US5364711A (en) * | 1992-04-01 | 1994-11-15 | Kabushiki Kaisha Toshiba | Fuel cell |
| JPH0676852A (en) * | 1992-08-31 | 1994-03-18 | Sanyo Electric Co Ltd | Portable power source |
| US6777118B2 (en) * | 2001-01-24 | 2004-08-17 | Casio Computer Co., Ltd. | Power supply system, fuel pack constituting the system, and device driven by power generator and power supply system |
| JP2003036879A (en) * | 2001-07-19 | 2003-02-07 | Casio Comput Co Ltd | Power system |
| WO2004004049A1 (en) * | 2002-06-28 | 2004-01-08 | Nec Corporation | Fuel cell and method of use teereof |
| JP2010108938A (en) * | 2009-11-06 | 2010-05-13 | Casio Computer Co Ltd | Fuel container |
| JP2010114083A (en) * | 2009-11-06 | 2010-05-20 | Casio Computer Co Ltd | Fuel container |
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