JPS60117562A - Alkali-matrix-type hydrogen-oxygen fuel cell - Google Patents

Alkali-matrix-type hydrogen-oxygen fuel cell

Info

Publication number
JPS60117562A
JPS60117562A JP58226579A JP22657983A JPS60117562A JP S60117562 A JPS60117562 A JP S60117562A JP 58226579 A JP58226579 A JP 58226579A JP 22657983 A JP22657983 A JP 22657983A JP S60117562 A JPS60117562 A JP S60117562A
Authority
JP
Japan
Prior art keywords
electrolyte
water
negative electrode
water absorption
absorption plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP58226579A
Other languages
Japanese (ja)
Other versions
JPH0247061B2 (en
Inventor
Hisashi Kudo
工藤 寿士
Yuko Fujita
藤田 雄耕
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.)
Japan Storage Battery Co Ltd
Nihon Denchi KK
Original Assignee
Japan Storage Battery Co Ltd
Nihon Denchi KK
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 Japan Storage Battery Co Ltd, Nihon Denchi KK filed Critical Japan Storage Battery Co Ltd
Priority to JP58226579A priority Critical patent/JPS60117562A/en
Publication of JPS60117562A publication Critical patent/JPS60117562A/en
Publication of JPH0247061B2 publication Critical patent/JPH0247061B2/ja
Granted 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
    • H01M8/04082Arrangements 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
    • H01M8/04119Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
    • 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
    • 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 prevent any voluminal changes of electrolyte by installing a water absorption plate so that it is in close contact with the back surface of the negative electrode. CONSTITUTION:A porous sintered nickel plate which is termed a water absorption plate 4 and does not hold any electrolyte is installed in close contact with the back surface of a negative electrode. A steam gas the temperature of which is controlled so that it has a partial steam pressure equal to the vapor pressure of 30% aqueous potassium hydroxide solution in the battery when the atmosphere becomes saturated is supplied to a hydrogen gas chamber 11. A part of the steam gas is supplied to a negative electrode 2 through the holes 6 and the hydrogen gas paths 5 of the water absorption plate 4. When the battery is discharged, oxygen and hydrogen are consumed in each electrode and water is produced at the interface between the electrolyte and the negative electrode 2. Accordingly, although electrolyte contained in the matrix expands and tends to leak out through the fine holes of the electrode, the increased amount of electrolye is absorbed by the water absorption plate 4. Therefore it is possible to prevent any voluminal changes of the electrolyte.

Description

【発明の詳細な説明】 本発明は燃料電池特にアルカリマトリックス7(11水
索−酸素燃料電池の改良に係り、イの[1的どりるとこ
ろは電池の放電生成物である水を過不足なく系外へ除去
し得る方法を提供セ、/υど°ケるにある。1アルカリ
マトリックス型水木−酸系燃tHI曲は電解液となる水
酸化カリウl)水溶液を保持ざIしたシート状のアスベ
ストマトリックズの両10Iに金。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the improvement of fuel cells, particularly alkaline matrix 7 (11 water line-oxygen fuel cells), and the objective of the present invention is to ensure that water, which is a discharge product of the battery, is used in an appropriate manner. Provides a method that can remove it from the system. 1) Alkaline matrix water-acid fuel tHI is a sheet-like material that holds an aqueous solution of potassium hydroxide, which serves as an electrolyte. Gold on both 10I of asbestos matrix.

白金、!@あるいはパラジウムブラックを触媒どJる正
4セど負極とを密着さ【!−1電極のtテ面にはイれぞ
れ酸化剤とくする酸素ど燃料どなる水素とを供給するた
めのガス卒を右する構造からなっている。
platinum,! @Or use palladium black as a catalyst and place the positive, 4 and negative electrodes in close contact. The t-side of the -1 electrode has a structure for supplying gases for supplying an oxidizing agent, oxygen, fuel, and hydrogen, respectively.

電池の起電反応(71次のとおりである。The electromotive reaction of the battery (71) is as follows.

止極テ1/ 2021−1−120+2e→21−10
− ・・、・(1)負極で H2+20 H−→21−
l 20 +2e ・・・(2)全体で1/ 202−
1−1−+ 2→l−120・・・(3)(3)式から
明らかなように、この電池では電極反応の進行に伴4に
い水が生成するので、電池を安定して作vJさけるため
には生成水を系外へ迅速に除去しな(プればならない。
Stop pole Te1/2021-1-120+2e→21-10
− ・・・(1) At negative electrode H2+20 H−→21−
l 20 +2e ... (2) Total 1/202-
1-1-+ 2→l-120... (3) As is clear from equation (3), in this battery, 4 water is generated as the electrode reaction progresses, so the battery cannot be operated stably. In order to avoid VJ, the produced water must be quickly removed from the system.

〈2)式から]リレらかなように、水の生成は負極側で
起るので、生成水の除去は負極側で行なうのが好jl 
l、 <、一般に負極背面から水素ガス流中へ蒸発さU
る方法がとられる。
[From equation 2] As it is clear, water generation occurs on the negative electrode side, so it is preferable to remove the generated water on the negative electrode side.
l, <, U is generally evaporated from the back of the negative electrode into the hydrogen gas flow.
A method is taken to

このlll’i、牛成し1c水だ(プが蒸発して電解液
の水が蒸Yi’: L/ <’r−,いようにり′るた
めに、水素は電解液の飽和水1′A気り下と同じ水蒸気
圧を持つように湿度調整されたIN2、電池に供給され
る。
This lll'i is 1 c of water. 'A IN2, whose humidity is adjusted to have the same water vapor pressure as under the air, is supplied to the battery.

一方、水の生成iiiはIA min当り5.6111
CI テ、その生成速度は電池に流れる電流に比例゛す
る。従って電池の負荷電流が急激に変動する場合、例え
ば5Δ/ d+aの小さな放電電流密面か1う突然3!
iA、’<IIItの大電流での放電に移行した場合、
水の生成速度(ま28mQ / zlut 、l1li
n か ら 196mQ / +、lul 、m!n 
へ危檄に増大する。f1極f17面からの水の蒸発外f
αが水生成速度に追いつかイrい1易合に(、;、電W
(液11が増大しやがて正・負両電極の細孔り目−1r
lfiF+’r il&がilll lliすることに
ケる。
On the other hand, water production iii is 5.6111 per IA min
The rate of CI production is proportional to the current flowing through the battery. Therefore, when the load current of the battery fluctuates rapidly, for example, a small discharge current density of 5Δ/d+a or 1 suddenly 3!
When transitioning to discharging with a large current of iA,'<IIIt,
Water production rate (28mQ/zlut, l1li
n to 196mQ/+, lul, m! n
The situation is increasing alarmingly. Water evaporation from f1 pole f17 plane f
It is easy for α to catch up with the water production rate (, ;, electric W
(As the liquid 11 increases, the pores of both the positive and negative electrodes -1r
It turns out that lfiF+'r il& is ill lli.

従来、上記の負荷変動に伴イI−う電解液量の変11′
1を補償するために、電解液貯蔵板ど称される’fl’
f VIY液を保持させた多孔性焼結ニラ))ル(反を
負極の背面に密キzざ1±、マトリックス中の電解液と
貯蔵板中の電wI液とを負極の細孔を通じて連通さt!
るという方法が提案されている。
Conventionally, the change in the amount of electrolyte caused by the above-mentioned load fluctuation 11'
1, the electrolyte storage plate is called 'fl'
f A porous sintered chive that holds the VIY liquid)) (the opposite side is placed on the back side of the negative electrode with dense scratches 1±), and the electrolyte in the matrix and the electrolyte in the storage plate are connected through the pores of the negative electrode. Let it pass!
A method has been proposed.

かかる構成の電i14では、il d:+が急激に:1
・1人しく水の蒸発速度が生成速度に)Gい−)か(4
: り41−るど、マトリックス中の増加しl、二重V
f(ilセが(1(4ス0) 8111 fl、4通っ
で電解液貯蔵板へ移ΦI+−!Jる。、 ”1. シC
、、C’h A:+が小さくなって水の蒸発外+Ctが
11成辻11〕をり、 :I: 0イ)ようになると、
71ヘリツイ7ス中の電解液けが減少してくるの(、′
>1’Jは貯蔵中の電解液が(コ(→Sの細孔を通−)
−(、”7 l・リツクスの方へ移動する。
In the electric i14 with such a configuration, il d:+ suddenly becomes:1
・The evaporation rate of water is the production rate)G-) or (4
: 41-rd, increasing l in matrix, double V
f(il se is (1 (4s 0) 8111 fl, transferred to the electrolyte storage plate in 4 passes ΦI+-!J., "1.
,,C'h A:+ becomes smaller and the water evaporation +Ct becomes
The amount of electrolyte in the 71 Heli Twist 7 is decreasing (,'
>1'J means that the electrolyte in storage is
-(,”7 Move towards Lricks.

この、1.う(に電解液貯蔵板に1電池の急激<r M
 Wl変動(、二電1.Iう゛d1解欣の体積変化を補
償づる働さをりる。
This, 1. (The sudden drop of one battery to the electrolyte storage plate <r M
It works to compensate for the volume change of Wl fluctuation (2D 1.I = d1).

しかし、貯メル様の背後に(:I水素が流れているため
貯i+Q ill ’l目り電解8kが飛沫と2.、て
水素ガス中にM人すイ、I−ど(,1;す口Jらねイ〔
いうえ、人さイr負荷がlff1115間続ζ31、)
Si i、9合には、貯蔵板が電解液で充満し、やh(
゛(貯蔵板から電解液が漏出することにイ「る5、かか
る現象は電解液の濃度を低下させ、電;1−電圧の劣化
をひき起1J、更に、かかる電池で(、′I生成水が?
1′i解散ど」(にマトリックスから貯蔵板へ、(Iつ
るいは貯i−■板から71〜リツクスヘ移動するので、
、71〜11ツクス中の電解液)閃mは刻々変化する。
However, behind the hydrogen gas (:I hydrogen is flowing, there are electrolytic 8k droplets and 2., and there are M people in the hydrogen gas. Don't say it [
In addition, the human load is lff1115 intermittent ζ31,)
At Si i, 9, the storage plate is filled with electrolyte, and h(
``(Leakage of the electrolyte from the storage plate) 5. Such a phenomenon reduces the concentration of the electrolyte and causes a deterioration of the electric voltage. Water is?
1'i dissolves () from the matrix to the storage board, (I moves from the storage i-■ board to 71 ~ Rix, so
, 71-11) The flash m changes every moment.

それ、I、(山ハ、! illの、1、い安定した放電
電圧を得ることはむ・1”かしい。
It's difficult to obtain a stable discharge voltage.

本発明に1、従メ(アルカリマトリックス型水素−酸素
燃P1電池がbつ上;ホの如き欠点を除去1!んどする
ーbの“Cある。、 Iil’l ”>、本発明は水吸
収板と称ずべき、電解液を保持しない髪孔1’l焼結−
ツ//J1・(反を負極背面に密着させて配し、X11
 M液どC1捧との界面′C−1戊覆る水だけを該水吸
収1〜に吸いとることに、1:す、電解液の体積変化を
防が/υど−Jと、bのである。
The present invention has the following advantages: 1. The present invention has the following advantages: A 1'l sintered hair pore that does not retain electrolyte and can be called an absorbing plate.
TS//J1・(Place the opposite side in close contact with the back of the negative electrode,
By absorbing only the water that covers the interface between the M liquid and C1 into the water absorption 1~, 1: prevents the volume change of the electrolyte solution/υdo-J and b. .

なd3、生成水II−[III<吸Ill<板(1:吸
いとI)れl、1胃ン。
d3, produced water II-[III<suction Ill<plate (1: suction and I), 1 stomach.

該吸収板から水素ガス流中へ然介]ノ、未反応水先ガス
と」(に系外へ1)1出される。
From the absorption plate, unreacted pilot gas is discharged into the hydrogen gas stream (1) out of the system.

以下、本発明の一実施例を図面(、二γnっで1述・す
る。
An embodiment of the present invention will be described below with reference to the drawings.

第1図は本発明にかかるアルJ、r IIントリツィl
々型水素−酸素燃料電池の単セルjit本(11冒告図
(・ル);)、図に於いて、(1)及び(2)は銀−バ
ラン・°111ブラックをポリ 4フツ化エチレンを結
着剤としく100メツシコニツケル網に糊塗した厚さ0
.3mmの1棒及び負極、(3)は電解液となる30w
t%水酸化カリウム水溶液を保持ざ1!′たIlざ0,
5mmのアスベストマトリックス、(4)は(1極(2
)の背面に位71 L、負極側の片面に水素ガスの通路
どなる凹部(5)ど該凹部並びに負極へ水素ガスを供給
、I゛るI、^すC11,’llff1 (fi)とを
右する多孔f1焼結ニッケル板か’−) /、i:る1
−/さ1mmの水吸収板、(7)及び(7′)はニラタ
ルボキスバンド網から<7る集電網、(11)及び〈8
′)はステンレススチール板から4−る集″c1゛(枚
、(9)及び(9′)は電池温度を 定(1−保つlこ
めに冷媒が流されるポリ4jルフ4ン樹脂製のクーラン
トル−1〜である。、M索ガス室(10)は行さどまり
になっていて、酸素ノfス(,1消費さIl、 7;:
 ht 1、’+1が供給される。一方、水素ガス室(
11)に(,1,電解液の30%水酸化カリウム水溶液
のI:q和水蒸気11に等しい水蒸気圧を持つよう(、
:、tlnl Iu調11゛Cされ!、:水素ガスが供
給され、その一部(L水成11M板(4)の貫通孔(6
)及び水素ガス通路(5)を通・)C(1極(2)へ供
給される。
FIG.
In the figure, (1) and (2) are silver-balun °111 black and polytetrafluoroethylene. Thickness 0 glued on 100 mesh nickel mesh as a binder.
.. 1 rod of 3mm and negative electrode, (3) is 30W which will be the electrolyte
Hold t% potassium hydroxide aqueous solution 1! 'TaIlza0,
5mm asbestos matrix, (4) (1 pole (2
) On the back side of 71 L, there is a recess (5) with a hydrogen gas passage on one side of the negative electrode.Hydrogen gas is supplied to the recess and the negative electrode. Porous f1 sintered nickel plate?'-) /, i:ru1
- / water absorption plate with a diameter of 1 mm, (7) and (7') are current collector nets made from Niratalbokkis band net, (11) and <8
(9) and (9') are polyurethane resin coolants into which coolant is flowed to keep the battery temperature constant (1). The M cable gas chamber (10) is at a standstill, and the oxygen supply (,1 is consumed Il, 7;:
ht 1,'+1 is supplied. On the other hand, the hydrogen gas chamber (
11) to have a water vapor pressure equal to (,1, I:q water vapor of 30% potassium hydroxide aqueous solution as electrolyte solution, 11).
:, tlnl Iu tone 11゛C! , : Hydrogen gas is supplied, and a part of it (through hole (6) of L Hydrogen 11M plate (4)
) and hydrogen gas passageway (5). ) C (1 pole (2) is supplied.

この電池を放電IJると、各々の電極で酸素及び水素が
消費されると同時に、電解液と負極(2)どの71面C
水が/1成する1、それ故、マ[−リックス中の電IW
)々lk体槓膨1!14 Lノて電極の細孔がら漏出1
ノ、1、うど(Jイνが、水吸収板(4)がキャピラリ
ー効!J!で電F/I! 81iのI11加分を吸いと
るので、電解液が休積変化することはSiい。ここでン
1目すべきは、水吸収板に吸いとられる液体は電解液の
最外端部、つJす、生成したばかりの水だLJであるj
:、(である3゜また、水の/1−成速度に比1)多孔
11焼結ニツケル抛の水吸収速段が極めて速いのて゛、
水;17I成(1ろ亡い/2や吸11!仮に吸いとられ
、グ1成速1すの変化、Iθ!普Jれば負荷変動に関係
4i (宙Vf(液の棒積Xゝ)淵1(°)(ま常に一
定に1にたれる点である。
When this battery is discharged, oxygen and hydrogen are consumed at each electrode, and at the same time, the electrolyte and the negative electrode (2)
Water forms /1, therefore, the electric current IW in the matrix
) 1k body swelling 1!14 Leakage from the pores of the L electrode 1
ノ, 1, Udo (J I ν is the capillary effect of the water absorption plate (4)! J! absorbs the I11 addition of 81i, so it is impossible for the electrolyte to undergo a dead volume change. The first thing to note here is that the liquid absorbed by the water absorption plate is the outermost part of the electrolyte, and the water that has just been generated is LJ.
:,(3°) Also, since the water absorption speed of the porous 11 sintered nickel rod is extremely fast,
Water; 17I formation (1 loss / 2 and suction 11! If it is absorbed, the change in G1 growth rate 1su, Iθ! Normal J is related to load fluctuation 4i (Air Vf (liquid bar volume ) Abyss 1 (°) (This is a point that always dips to 1.

更に、−[]吸収板に吸いとられた水(Jイの後水系ガ
ス中へ蒸発するわけであるが、この蒸発1;L )1ス
どの接触表面積が極めて大きい多孔板から、17かも純
水の蒸発であるため、その外1αμ極めて速く、吸収板
が水で充満覆ることは<1い。
In addition, the water absorbed by the -[] absorption plate (after this evaporation into the water-based gas, 1; L) 17 is also pure from the perforated plate, which has an extremely large contact surface area. Since water evaporates, it is extremely fast (1αμ), and it is unlikely that the absorption plate will be filled with water.

このように本発明にかがる電11!! t;=於τ1.
1. 、 ’l’ l〜。
In this way, 11 electricity is applied to the present invention! ! t;=atτ1.
1. , 'l' l~.

水は迅速に水吸収板に吸いと”l JL I市解dkL
I)捧伯亡wA度が変化号ることはないのぐ、山現竹の
、1い安定した電r1が得られると同+1.’iに、水
吸収板中L−tlNlN解合まれないので、水系)fス
中に゛市TM液q)飛沫が混入することも4丁い、。
Water is quickly absorbed into the water absorption plate.
I) There is no change in the degree of dedication, but if a stable electric r1 of 1 is obtained from Yamagentake, the same +1. Also, since the L-tlNlN is not dissolved in the water absorption plate, droplets of the Ichi TM liquid q) may get mixed into the water system.

次に本発明の効果を確かめろIこめに、電極作用面積が
1(lτ11の1イ)1図に示づよう4r電池を11ず
ノて放電試験1.. /、−結1(について述べる。
Next, to confirm the effect of the present invention, a discharge test 1 was conducted using a 4R battery with an electrode action area of 1 (lτ11's 1A) as shown in Figure 1. .. /, -Conclusion 1 (described below.

第′L1図11電ill! H+、’t ILLを80
℃どし、80℃での潤度が11 、7 Q6にイー’、
 K) J、−)に加湿した水素を800cc /mi
nのj”、l lCj ’−(”供r:HL、イIがf
)20△で100時間の定電流h(電を1.lごII、
’iの?1′i池電圧の11(移を示す図であるが、J
l”ii! I’−安定1ツノ、:電nが(!1られ、
本弁明の水成117板が有効に作用しくいることが(r
証された。
'L1 Figure 11 Electric ill! H+,'t ILL 80
The humidity at 80℃ is 11,7 Q6 is E',
K) J, -) humidified hydrogen at 800cc/mi
n's j", l lCj '-("supply r:HL, iI is f
) 20△ for 100 hours at a constant current h (current of 1.l)
'i's? This is a diagram showing the 11 (transition) of the 1'i cell voltage, but J
l"ii! I'- stable one horn, : electric n is (!1
It is clear that the Suisei 117 board of this defense works effectively (r
It was proven.

第3a+ IJ、1.’ !it! fh i’ljj
を!i八へ20分、20△テ20分のに’l電を繰;!
g ’JJL11変動試験結果であり、電池電圧1に:
暑21! 21:イコkji塾HiF+Jに対しても極
めて鋭敏に応答し、か″)各/Zのh’l ?1’l壮
(流での電圧は非常に安定していlc3、 +111.− 、い・1′わの試験に於てら1末反応水
素カスどl’宙“111;かC’s III出された水
は完全に純水で、電解液イI含・11こと【、1イrか
った。
3rd a+ IJ, 1. '! It! fh i'ljj
of! 20 minutes to i8, 20 minutes to 20△te, repeat 'l electric;!
g 'JJL11 fluctuation test results, battery voltage 1:
Hot weather 21! 21: It also responds extremely sharply to Ikokji Juku HiF+J, and the voltage at each /Z h'l ?1'l So (current voltage is very stable lc3, +111.-, I 1. In my test, the water that came out of the hydrogen sludge in the air was completely pure water, and contained an electrolyte solution. Ta.

Ωの/、Tめ、この電池で負極背面の水吸収板をと9)
八−+ (−j験し11=どころ、両)fス室に電解液
が漏出し1.−、 tl)I−どl)目)し本発明にJ
:ろ水吸収板が11−成木を吸いt!: =)−’r電
解液のイホ栢あるい(J濃度を常に一定に保っているこ
とが明らかになっIS。
Ω/, T, this battery has a water absorbing plate on the back of the negative electrode9)
8-+ (-j test 11=dori, both) Electrolyte leaked into the f chamber 1. -, tl) I-dl) and the present invention J
: The filtrate absorbing board sucks 11-mature trees! : =)-'rIt became clear that the concentration of the electrolyte was always kept constant.

なお、本発明の水成11!板に用いる多孔性焼結ニッケ
ル板の軸孔径は1〜10μ、好ましくは2〜6μに孔径
分布のピ〜りを有するものがにい3.また、水素ガスを
f共給するだめの貫通孔の径とし°rt、t。
In addition, Mizusei 11! of the present invention! The axial hole diameter of the porous sintered nickel plate used for the plate is 1 to 10μ, preferably 2 to 6μ, and has a pore size distribution with a peak.3. In addition, the diameter of the through hole for co-feeding hydrogen gas is rt and t.

、5〜1.OIllmのものが適当である。, 5-1. OIllm is suitable.

以F訂)ホした如く、本発明にかかるアルカリマ!〜リ
ツクスを水系−11!i素燃1′21電れ!I l:L
 、Ci捧背而面、1 ’j%’!着するように水吸収
板を配′ζ;るこ、1・(二、J、 l’l 、 ?t
i油の放電反応により生成する水だ(jろ吸い31・e
)、迅速に系外へ除ムするものぐあり、でのT業的1l
Ill値は極めて人である。
(edited by F) As shown above, Alkalima according to the present invention! ~Water-based Ricks-11! i Somen 1'21 Electricity! I l:L
, Ci dedication, 1 'j%'! Arrange the water absorbing plates so that the water absorbs the water.
i It is water generated by the discharge reaction of oil (j filtration 31, e
), there is something that can be quickly removed from the system, and it is a T-business 1l.
The Ill value is extremely human.

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

第1図は本発明にかかるアルカリマトリックス型水索−
酸素燃判電池の単セルの基本4flf 3ろ図で、偽る
。第2図及び第3図は、本発明にかかるアルカリマ]〜
リツクス型水索−酸素燃判電れ(シの放電特tqを示1
1図であり、第2図1,1、電流1谷1920Δ、、/
 、lぜ11の定電流放電R牲を、第3図(L電流密1
0 ;]△7・詞で2()分、20Δ/ clntで2
0分の放電を繰返り負イ111変動特(IIを小り。 1・・・■極、?・・・(1極、3・・・水酸化カリウ
ム電解液を保持さけに〕′スベストマトリックス、4・
・・ホ1坂11v板、!1・・・水系ガス通路、6・・
・貫通孔、 7,7′・・・東電網、8.8′ ・・・
集電板、9,9′ ・・・クーラ汀 1 図 方 7 図 A 3 閃 / 2 3 T!rT 向 (i)
Figure 1 shows an alkali matrix water cable according to the present invention.
The basic 4flf 3 diagram of a single cell of an oxy-fuel battery is false. FIG. 2 and FIG. 3 show Alkalima according to the present invention]
Lix-type water cable - Oxygen fuel discharge characteristics
Figure 1, Figure 2 1, 1, current 1 valley 1920Δ, /
Figure 3 (L current density 1
0;]△7・2() minutes for words, 2 for 20Δ/clnt
Repeat the discharge for 0 minutes, and the negative a 111 fluctuation characteristic (II is decreased. 1...■pole, ?...(1 pole, 3...to avoid holding the potassium hydroxide electrolyte)'Sbest Matrix, 4.
... Ho1zaka11v board! 1... Water-based gas passage, 6...
・Through hole, 7,7′...Tokyo Electric Network, 8.8′...
Current collector plate, 9,9'...Cooler plate 1 Figure 7 Figure A 3 Flash/2 3 T! rT direction (i)

Claims (1)

【特許請求の範囲】[Claims] 1、片面に多数の四部と凸部とをイjし、他面J:り該
凹部に貫通する多数の穿孔をf]りる多孔竹焼粘ニッケ
ル板からなる水吸収板の前記凸部を、水系極のガス極側
に密着するにうに配したことを特徴とするアルカシマ1
〜リツクス型水素−′M素燃tζ[Wi池。
1. A water absorbing plate made of a porous bamboo-fired nickel plate with a large number of four parts and a convex part on one side, and a large number of perforations penetrating the concave parts on the other side. , Alcashima 1, which is characterized by being arranged on the side of the aqueous electrode that is in close contact with the gas electrode side.
~Rix-type hydrogen-'M elementary fuel tζ [Wi Pond.
JP58226579A 1983-11-29 1983-11-29 Alkali-matrix-type hydrogen-oxygen fuel cell Granted JPS60117562A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58226579A JPS60117562A (en) 1983-11-29 1983-11-29 Alkali-matrix-type hydrogen-oxygen fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58226579A JPS60117562A (en) 1983-11-29 1983-11-29 Alkali-matrix-type hydrogen-oxygen fuel cell

Publications (2)

Publication Number Publication Date
JPS60117562A true JPS60117562A (en) 1985-06-25
JPH0247061B2 JPH0247061B2 (en) 1990-10-18

Family

ID=16847376

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58226579A Granted JPS60117562A (en) 1983-11-29 1983-11-29 Alkali-matrix-type hydrogen-oxygen fuel cell

Country Status (1)

Country Link
JP (1) JPS60117562A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000215902A (en) * 1999-01-27 2000-08-04 Toyota Motor Corp Gas separator for fuel cell, fuel cell and manufacture of gas separator for fuel cell
CN1311583C (en) * 2002-07-30 2007-04-18 高能量有限公司 Suspensions for use as fuel for electrochemical fuel cells
JP2008198567A (en) * 2007-02-15 2008-08-28 Nippon Soken Inc Fuel cell

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR940007757Y1 (en) * 1991-11-14 1994-10-24 금성일렉트론 주식회사 Semiconductor package

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000215902A (en) * 1999-01-27 2000-08-04 Toyota Motor Corp Gas separator for fuel cell, fuel cell and manufacture of gas separator for fuel cell
CN1311583C (en) * 2002-07-30 2007-04-18 高能量有限公司 Suspensions for use as fuel for electrochemical fuel cells
JP2008198567A (en) * 2007-02-15 2008-08-28 Nippon Soken Inc Fuel cell

Also Published As

Publication number Publication date
JPH0247061B2 (en) 1990-10-18

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