JPS58164154A - Electrolyte impregnating method of fuel cell - Google Patents

Electrolyte impregnating method of fuel cell

Info

Publication number
JPS58164154A
JPS58164154A JP57047992A JP4799282A JPS58164154A JP S58164154 A JPS58164154 A JP S58164154A JP 57047992 A JP57047992 A JP 57047992A JP 4799282 A JP4799282 A JP 4799282A JP S58164154 A JPS58164154 A JP S58164154A
Authority
JP
Japan
Prior art keywords
vacuum
electrolyte
block
condition
heating furnace
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
JP57047992A
Other languages
Japanese (ja)
Inventor
Nobuo Miyoshi
三好 信雄
Hiroyuki Tajima
田島 博之
Masahiro Sakurai
正博 桜井
Atsuo Watanabe
敦夫 渡辺
Tomoyoshi Kamoshita
友義 鴨下
Toshihiro Sugiyama
杉山 智弘
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.)
Kansai Electric Power Co Inc
Fuji Electric Co Ltd
Original Assignee
Kansai Electric Power Co Inc
Fuji Electric Co Ltd
Fuji Electric Manufacturing 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 Kansai Electric Power Co Inc, Fuji Electric Co Ltd, Fuji Electric Manufacturing Co Ltd filed Critical Kansai Electric Power Co Inc
Priority to JP57047992A priority Critical patent/JPS58164154A/en
Publication of JPS58164154A publication Critical patent/JPS58164154A/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
    • H01M8/04276Arrangements for managing the electrolyte stream, e.g. heat exchange
    • H01M8/04283Supply means of electrolyte to or in matrix-fuel cells
    • 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

Landscapes

  • Fuel Cell (AREA)
  • 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)

Abstract

PURPOSE:To impregnate the electrolyte fully into a matrix by degassing a fuel cell fully at a high temperature then feeding the electrolyte and maintaining the condition for a long time. CONSTITUTION:A fuel cell block 8 laminated with a plurality of unit cells is installed in a vacuum heating furnace 9 horizontally or at a slight inclination. The block 8 is heated to 70-120 deg.C under this condition, then the vacuum heating furnace 9 is degassed fully to the degree of vacuum of 5mm. Hg or less. This condition is maintained for a fixed time, then the electrolyte 11 heated to 70- 120 deg.C and vacuum degassed is gradually fed into the block 8 from an external heating tank 10 so as to fill the block 8 fully. Next, the atmosphere in the vacuum heating furnace is maintained at a vacuum and high temperature under the condition that the electrolyte is held in the block 8. Then, a valve 13 is opened under the condition that the atmosphere in the vacuum heating furnace 9 is kept at a vacuum and high temperature, and the electrolyte being held in the block 8 is discharged to an external tank 14 with the same degree of vacuum as that of the vacuum heating furnace 9. After the electrolyte has been fully discharged, the dry air is fed through a valve 15 so as to attain a normal pressure condition.

Description

【発明の詳細な説明】 本発明は、電解質固定型燃料電池のマトリツクスに電解
質を含浸する方法番こ関する。燃料電池のマトリックス
に電解質を含浸する場合、燃料と空気の混合を防ぐため
にマトリックスの空隙を元金に電解質で充満させる必要
がある0 この植の燃料電池は、一般に第1図に示す構成の単電、
池を積層してなる。すなわち、燃料g亀の単電池は、ア
ノード11カソード3、両電極に挟持された非喝子電導
性で多孔性を有する部材(マトリックス)2、ならびに
、集電およびガスの混合を防ぐセパレータプレート4を
図示の朧序で積層した構造である。電礁の拡大図を第2
図に示す。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for impregnating an electrolyte into a fixed electrolyte fuel cell matrix. When the matrix of a fuel cell is impregnated with an electrolyte, it is necessary to fill the voids in the matrix with the electrolyte to prevent mixing of fuel and air. Electric,
The ponds are layered. In other words, the unit cell of the fuel turtle includes an anode 11, a cathode 3, a non-conductive and porous member (matrix) 2 sandwiched between both electrodes, and a separator plate 4 that prevents current collection and gas mixing. It has a structure in which these are layered in the vague order shown in the diagram. Second enlarged view of the reef
As shown in the figure.

7ノード@lとカノードs3は、ともに炭素繊−を紙状
にすいたカーボン#16を基材として白金触轟を担持し
た炭sym車から成る触媒層7を塗布積層した構造であ
り、マトリックス2は粒径約≦、5声諷の粉末を自有し
たものである。
Both the 7 node @l and the canode s3 have a structure in which a catalyst layer 7 consisting of a carbon sym wheel carrying a platinum catalyst is coated and laminated using carbon #16 made of paper-like carbon fibers as a base material, and the matrix 2 The powder has a particle size of approximately 5 tones.

マトリックス2に電解質としてりん酸電解液を含浸する
場合、以下の問題がある0すなわち、燃料電池の鴫S痕
は通常高#I嵐のものが使用され、粘度は砲めて轟い。
When the matrix 2 is impregnated with a phosphoric acid electrolyte as an electrolyte, there are the following problems. Namely, the fuel cell stain is usually used with a high #I storm, and the viscosity is extremely high.

II3図に:装置10G−のリン酸の帖駅一温度の関係
を示す、この高粘度のために、電S*fr!トリックス
に含浸するための毛細管効果が低く、電解液のマトリッ
クス内部への浸透遍腋が偽めて遅くなる。又、電解液が
高粘度であるため、電解液中の気体が外部に放出されに
くい◎−万、マトリックスを構成する素材の粒子形状は
一足でなく、電lI#液が均一な速度で含浸されないの
で、マトリックス内に気泡が浅域し易くなる。
Figure II3 shows the relationship between the temperature of phosphoric acid in the device 10G, and due to its high viscosity, the electric S*fr! The capillary effect for impregnating the matrix is low, and the penetration of the electrolyte into the interior of the matrix is falsely slow. In addition, because the electrolyte has a high viscosity, the gas in the electrolyte is difficult to release to the outside.◎-The particle shape of the material that makes up the matrix is not uniform, and the electrolyte is not impregnated at a uniform rate. Therefore, bubbles tend to form in shallow areas within the matrix.

このように、マトリックスに必要十分な量の電′S漱を
含浸することは6易でなく一燃料と空気の混合を生ずる
t険や、燃料電池の特性低Yなどを生じ易くなる。
As described above, it is difficult to impregnate the matrix with a necessary and sufficient amount of S-sodium, leading to problems such as mixing of fuel and air and poor characteristics of the fuel cell.

本@明は、域解漱のかかる性貞に−みて、成好な含浸方
法をIs供することをI的とするもので、温度を高める
ことで電解液の粘度を低下させ、マトリックス番こ含浸
するための毛細管効果を^めるとともに、マトリックス
と域解葭を脱スして気泡の電解gを所定の場所に含浸す
る方式を確立し、燃料電池の出力特性の安定性を−保す
る効果を得るものである。
The purpose of this book is to provide a successful impregnation method in view of the nature of regional dissolution and rinsing. In addition to increasing the capillary effect for the fuel cells, we have established a method of removing the matrix and the molten reeds and impregnating the predetermined locations with the electrolytic gas of bubbles, which is effective in maintaining the stability of the output characteristics of the fuel cell. This is what you get.

第4図はこの発明の実施例を示すものである。FIG. 4 shows an embodiment of the invention.

第1図の単電池を複数積層した燃料電池のブロック8を
真空加熱炉9の中に水平又はわずかな傾きをもたせて設
置する。この状態でブロック8を70〜120℃の41
i−に昇温したのち、真空加熱炉9を十分な真空度(5
−Hf以下)に脱気する。この状−を一定時閾保った儀
、外部加温槽10より70〜IEOCK丼温し、かつ真
g!脱気した電S痕11をパルプ12を介して真空加熱
炉9円に導入し、ブーツク8内に徐々に供給する。eg
cl[の供給は、ブーツク8内に電S*が十分満たされ
た畿にパルプ13を閉じて停止する。この健、ブロック
8内に’III解痕を保持した状態で、真空加熱炉内の
XVa気を、6〜10■Hfの真空度と70〜120c
の温度として2〜10時閾保つ。その後、真空加熱炉9
内を5〜l G @@)1tの真空度と10〜120℃
の温度の雰囲気に保った状態でパルプ13を開き、ブー
ツク8内に保持した電解液を真空加熱炉9の箕!!!度
と同じ真空度にある外部槽14に排出する。
A fuel cell block 8 in which a plurality of unit cells are stacked as shown in FIG. 1 is installed in a vacuum heating furnace 9 horizontally or with a slight inclination. In this state, block 8 was heated to 41°C at 70 to 120°C.
After raising the temperature to i-, the vacuum heating furnace 9 is heated to a sufficient degree of vacuum (5
- Hf or less). After maintaining this state for a certain period of time, the external heating tank 10 heated the IEOCK bowl to 70°C, and the temperature reached 70°C. The degassed electric S trace 11 is introduced into a vacuum heating furnace 9 through the pulp 12 and gradually supplied into the boot stock 8. eg
The supply of cl[ is stopped when the pulp 13 is closed in the area where the boot stock 8 is sufficiently filled with electricity S*. In this case, while maintaining the 'III residual in the block 8, the
The temperature is maintained at the threshold of 2 to 10 o'clock. After that, the vacuum heating furnace 9
5 to 1 t of vacuum inside and 10 to 120℃
The pulp 13 is opened in a state where the atmosphere is kept at a temperature of ! ! It is discharged into an external tank 14 which has the same degree of vacuum as the temperature.

十分電解液を排出した後、乾燥気体をパルプ1Bから真
空m熱デ9の内部に供給して常圧状態とする・以上で真
空状態下での燃料電池に電解液を含浸する操作は終了す
る・ 以上述べたように、この発明によれば、燃料電池を4温
(70〜120℃)の丁で十分脱気した畿   ゝに、
鴫屏畝を供諭し、その状−を長時間保持するようにした
ため電′5tftをマトリックスに十分ζζ含浸するこ
とが9簡となる。
After sufficiently discharging the electrolyte, dry gas is supplied from the pulp 1B to the inside of the vacuum m-heating device 9 to create a normal pressure state.This completes the operation of impregnating the fuel cell with the electrolyte under vacuum conditions. - As described above, according to the present invention, the fuel cell is fully degassed at 4 temperatures (70 to 120 degrees Celsius).
Since the shape is maintained for a long period of time, it only takes 9 minutes to fully impregnate the matrix with 5 tft of electricity.

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

lI1図は単電池の11m図、累2園は電礁の側−拡大
図、gallはlIJ[1G(HIノリ/酸(D粘[’
l法図、lI4図は本発明の!lI施例のa*v!i7
!、置図である。 8・・・燃料電池ブロック、9・・・真空加熱炉、11
・・・電解液。 f 3 口 /4 1′4  口
The lI1 diagram is an 11m diagram of the single cell, the 2nd garden is an enlarged view of the side of the electric reef, and the gal is lIJ[1G (HI glue/acid (D glue)
The l law diagram and lI4 diagram are of the present invention! lI example a*v! i7
! , is an illustration. 8...Fuel cell block, 9...Vacuum heating furnace, 11
... Electrolyte. f 3 mouths/4 1'4 mouths

Claims (1)

【特許請求の範囲】[Claims] 電他間に電極リックスを挾持してなる単電池を有する燃
料電池において、真空加熱炉内で^諷状聰と十分な真空
度の下で燃料′tI/Laのマトリックスに高温の電解
質を供給し、さらに高温かつ十分な真空度の下でマトリ
ックスに電解質を含浸させることを特徴とする燃料電池
の電解質含浸方法。
In a fuel cell that has a single cell in which an electrode lix is sandwiched between electrodes, a high temperature electrolyte is supplied to a matrix of fuel 'tI/La in a vacuum heating furnace under a sufficient degree of vacuum. A method for impregnating an electrolyte in a fuel cell, which further comprises impregnating a matrix with an electrolyte at a high temperature and under a sufficient degree of vacuum.
JP57047992A 1982-03-25 1982-03-25 Electrolyte impregnating method of fuel cell Pending JPS58164154A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57047992A JPS58164154A (en) 1982-03-25 1982-03-25 Electrolyte impregnating method of fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57047992A JPS58164154A (en) 1982-03-25 1982-03-25 Electrolyte impregnating method of fuel cell

Publications (1)

Publication Number Publication Date
JPS58164154A true JPS58164154A (en) 1983-09-29

Family

ID=12790808

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57047992A Pending JPS58164154A (en) 1982-03-25 1982-03-25 Electrolyte impregnating method of fuel cell

Country Status (1)

Country Link
JP (1) JPS58164154A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02172158A (en) * 1988-12-26 1990-07-03 Asahi Chem Ind Co Ltd Impregnating method and equipment thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02172158A (en) * 1988-12-26 1990-07-03 Asahi Chem Ind Co Ltd Impregnating method and equipment thereof

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