JPH0326909B2 - - Google Patents
Info
- Publication number
- JPH0326909B2 JPH0326909B2 JP59153189A JP15318984A JPH0326909B2 JP H0326909 B2 JPH0326909 B2 JP H0326909B2 JP 59153189 A JP59153189 A JP 59153189A JP 15318984 A JP15318984 A JP 15318984A JP H0326909 B2 JPH0326909 B2 JP H0326909B2
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- water
- repellent
- gas diffusion
- diffusion 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.)
- Expired - Lifetime
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 57
- 239000005871 repellent Substances 0.000 claims description 20
- 238000009792 diffusion process Methods 0.000 claims description 13
- 239000010419 fine particle Substances 0.000 claims description 10
- 239000006185 dispersion Substances 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 5
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 13
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 13
- 239000004810 polytetrafluoroethylene Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 230000002940 repellent Effects 0.000 description 6
- 238000003860 storage Methods 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 230000007774 longterm Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000003350 kerosene Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical group FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical group FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical class C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8817—Treatment of supports before application of the catalytic active composition
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8803—Supports for the deposition of the catalytic active composition
- H01M4/8807—Gas diffusion layers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8878—Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body
- H01M4/8896—Pressing, rolling, calendering
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/96—Carbon-based electrodes
-
- 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
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Composite Materials (AREA)
- Inert Electrodes (AREA)
Description
[産業上の利用分野]
本発明は寿命が長く、かつ電気抵抗の小さなガ
ス拡散電極の製造方法に関するものである。
[従来の技術]
従来は特開昭48−55333のように、炭素粉末の
分散液と撥水性を有する結着剤の分散液とを混合
して、炭素粉末に決着剤の粒子を付着せしめ、ア
ルカリ処理、熱処理を施して炭素粉末と決着剤と
触媒物質を一体に結合するガス電極の製造方法が
あつた。また特開昭49−41830のように、結着剤
と撥水剤とを兼ねてポリテトラフルオロエチレン
(PTFE)粉末を用いるものであつた。
[発明が解決しようとする問題点]
空気電池等は貯蔵特性、高温高湿下での放電等
において、ガス拡散電極の撥水性が重要な問題点
である。PTFEの量を多くするとガス拡散電極の
ガス透過性が悪くなり作動電圧が低くなる。さら
にPTFE粉末を混合しているだけなので活性炭自
体撥水処理されていないため、長期貯蔵性が良好
でなかつた。また、液体もしくは固体撥水剤を溶
剤に溶かして活性炭に含浸させ、溶剤を蒸発させ
る製造方法もあつたが、撥水剤が活性炭の全表面
を覆い、電極の電気抵抗が大きくなるため、放電
作動電圧が低くなつた。また撥水剤の量を少なく
すると、充分な撥水効果が得られない欠点があつ
た。
本発明は撥水性の微粒子を活性炭表面に強固か
つ安定な状態で溶着させることにより、ガス拡散
電極の電気抵抗、接触能力を劣化せしめず撥水性
を持たせ、長期貯蔵特性を向上させるものであ
る。
[問題点を解決するための手段]
本発明の製造方法を説明する。
まず、活性炭もしくは触媒を吸着した活性炭を
水に分散せしめ、撥水性の微粒子の水性分散液を
水でうすめ、この分散液を適量滴下する。滴下す
る量は随時調節する。次に上記混合液を減圧しな
がら、活性炭表面に存在する微少な気泡を除きな
がら、活性炭表面に撥水性微粒子を含浸させ、
過乾燥する。次に微粒子の融点以上の温度で加熱
し、活性炭表面に撥水性の微粒子の一部を溶かし
て部分的に融着する。この後撥水処理した活性炭
と撥水性微粒子とを混合して、ローラーによりシ
ート化し、ニツケルネツトを圧着し、さらに撥水
性フイルムを圧着して、ガス拡散電極を製造して
いる。
[作用]
本発明は活性炭表面に吸着している気泡を減圧
により除去し加熱しているため、撥水性の微粒子
が均一に強固に活性炭表面に融着でき、電池の振
動、温度シヨツクに対して強くなり、さらに空気
との反応面積が拡がるため、大電流で使用でき、
長期貯蔵性が向上するものである。
[実施例]
本発明の実施例を説明する。
まず、触媒を吸着した活性炭100gを水1に
分散せしめ、次に径0.01〜50μのPTFEの60重量
%の水性分散液を、水で10倍にうすめ、活性炭分
散液に100ml滴下する。この滴下量はPTFE固形
分と活性炭との重量比が、活性炭を100とすると、
0.1:100〜40:100の間で良好な結果が得られる。
使用する活性炭の種類によつて上記範囲内で適宜
調整して用いる。次に上記混合液を40Torr〜
100Torrの減圧下で15分間撹拌し、活性炭表面に
存在する微少な気泡を除きつつ、その表面に
PTFEの微粒子を含浸させ、過乾燥する。さら
にPTFEの融点以上の温度380℃〜400℃で15分間
加熱し、活性炭表面にPTFEの一部を溶かして溶
着せしめる。融着は活性炭の全面を覆うのでな
く、活性炭を部分的に撥水化させるため、酸素還
元触媒の作用する表面は充分残つている。このよ
うにして撥水処理した活性炭80重量%とPTFE粉
20重量%とを混合し、ローラーによりシート化
し、ニツケルネツトを圧着し、さらにPTFEフイ
ルムを圧着して、ガス拡散電極を製造する。
上記のガス拡散電極を用いて試作した本発明に
よるPR44型空気電池[A]と、比較のため常圧
で混合し、融点以上の温度で加熱しないで製造し
たガス拡散電極を用いた同型の空気電池[B]
と、灯油にPTFEを溶解し活性炭と混合して灯油
を蒸発させてなるガス拡散電極を用いた同型の空
気電池[C]とを試作した。
初度の電池[A][B][C]の開路電圧、電池
の内部抵抗、0.9Vまでの放電容量、60%放電時
の作動電圧を表1に示した。また、温度45℃、湿
度60%中で、空気孔を開放して1ケ月貯蔵後の電
池の放電容量と放電作動電圧とを表2に示して比
較した。
[Industrial Application Field] The present invention relates to a method for manufacturing a gas diffusion electrode that has a long life and low electrical resistance. [Prior Art] Conventionally, as in JP-A No. 48-55333, a dispersion of carbon powder and a dispersion of a water-repellent binder are mixed, and particles of the binder are attached to the carbon powder. There has been a method for manufacturing gas electrodes in which carbon powder, a fixing agent, and a catalyst material are combined into one body through alkali treatment and heat treatment. Further, as in JP-A-49-41830, polytetrafluoroethylene (PTFE) powder was used as both a binder and a water repellent. [Problems to be Solved by the Invention] Water repellency of gas diffusion electrodes is an important problem in air batteries and the like in terms of storage characteristics, discharge under high temperature and high humidity, and the like. If the amount of PTFE is increased, the gas permeability of the gas diffusion electrode will deteriorate and the operating voltage will decrease. Furthermore, since the activated carbon itself was not water-repellent because it only contained PTFE powder, it did not have good long-term storage properties. Another manufacturing method was to dissolve a liquid or solid water repellent in a solvent and impregnate the activated carbon, and then evaporate the solvent, but the water repellent covered the entire surface of the activated carbon, increasing the electrical resistance of the electrodes and causing a discharge. The operating voltage has become low. Furthermore, when the amount of water repellent is reduced, a sufficient water repellent effect cannot be obtained. The present invention provides water repellency to the gas diffusion electrode without deteriorating its electrical resistance and contact ability by welding water-repellent fine particles to the surface of activated carbon in a strong and stable state, thereby improving long-term storage characteristics. . [Means for solving the problems] The manufacturing method of the present invention will be explained. First, activated carbon or activated carbon adsorbed with a catalyst is dispersed in water, an aqueous dispersion of water-repellent fine particles is diluted with water, and an appropriate amount of this dispersion is dropped. Adjust the amount to be dropped as needed. Next, while reducing the pressure of the above mixed liquid and removing minute air bubbles existing on the surface of the activated carbon, the surface of the activated carbon is impregnated with water-repellent fine particles,
Overdry. Next, the activated carbon is heated at a temperature higher than its melting point to melt and partially fuse the water-repellent particles to the surface of the activated carbon. Thereafter, the water-repellent activated carbon and water-repellent fine particles are mixed, formed into a sheet using a roller, a nickel net is crimped onto the sheet, and a water-repellent film is further crimped onto the sheet to produce a gas diffusion electrode. [Function] In the present invention, air bubbles adsorbed on the activated carbon surface are removed by reduced pressure and heated, so water-repellent fine particles can be uniformly and firmly fused to the activated carbon surface, making it resistant to battery vibration and temperature shock. It becomes stronger and the reaction area with air is expanded, so it can be used with large currents.
This improves long-term storage. [Example] An example of the present invention will be described. First, 100 g of activated carbon adsorbed with a catalyst is dispersed in 1 part of water, and then a 60% by weight aqueous dispersion of PTFE having a diameter of 0.01 to 50 μ is diluted 10 times with water, and 100 ml of the solution is added dropwise to the activated carbon dispersion. The amount of this dripping is based on the weight ratio of PTFE solid content to activated carbon, assuming that activated carbon is 100.
Good results are obtained between 0.1:100 and 40:100.
The amount is appropriately adjusted within the above range depending on the type of activated carbon used. Next, add the above mixture to 40Torr~
Stir for 15 minutes under a reduced pressure of 100 Torr to remove minute air bubbles on the surface of activated carbon.
Impregnate with PTFE particles and overdry. Further, the activated carbon is heated for 15 minutes at a temperature of 380°C to 400°C, which is higher than the melting point of PTFE, to melt and weld a portion of the PTFE to the surface of the activated carbon. The fusion does not cover the entire surface of the activated carbon, but only partially makes the activated carbon water repellent, so that a sufficient surface area remains for the oxygen reduction catalyst to act on. 80% by weight of activated carbon and PTFE powder treated with water repellency in this way
20% by weight, formed into a sheet using a roller, crimped with a nickel net, and further crimped with a PTFE film to produce a gas diffusion electrode. PR44 type air cell [A] according to the present invention was prototyped using the above gas diffusion electrode, and for comparison, the same type of air was mixed at normal pressure and manufactured using a gas diffusion electrode without heating at a temperature higher than the melting point. Battery [B]
We also prototyped the same type of air cell [C] using a gas diffusion electrode made by dissolving PTFE in kerosene and mixing it with activated carbon to evaporate the kerosene. Table 1 shows the open circuit voltage of the initial batteries [A], [B], and [C], the internal resistance of the batteries, the discharge capacity up to 0.9 V, and the operating voltage at 60% discharge. Table 2 shows the discharge capacity and discharge operating voltage of the battery after it was stored for one month at a temperature of 45° C. and a humidity of 60% with the air holes open for comparison.
【表】【table】
【表】
表1、2の結果から、本発明品は撥水性の微粒
子を融着しているが、特に貯蔵後の結果が放電容
量と放電作動電圧共に従来品[B][C]より優
れていることがわかる。
上記実施例では、撥水性の微粒子としてPTFE
を用いたガス拡散電極について記したが、この他
に4フツ化エチレンと6フツ化プロピレンとの共
重合体等のフツ素系樹脂を用いても、同様な製造
方法で優れた結果を得ることができる。
[効果]
以上のように、本発明のガス拡散電極は空気電
池に使用すれば、電池の内部抵抗が小さく大電流
使用に耐え、貯蔵後においても放電作動電圧、放
電容量等の優れた特性を得ることができる。[Table] From the results in Tables 1 and 2, the product of the present invention has water-repellent fine particles fused to it, but the results after storage are superior to the conventional products [B] and [C] in both discharge capacity and discharge operating voltage. You can see that In the above example, PTFE was used as the water-repellent fine particles.
Although we have described a gas diffusion electrode using fluoroethylene, excellent results can also be obtained using the same manufacturing method using other fluorocarbon resins such as copolymers of tetrafluoroethylene and hexafluoropropylene. Can be done. [Effects] As described above, when the gas diffusion electrode of the present invention is used in an air battery, the internal resistance of the battery is small and it can withstand high current use, and even after storage, it maintains excellent characteristics such as discharge operating voltage and discharge capacity. Obtainable.
Claims (1)
水性の微粒子分散液とを減圧下で混合し、乾燥
し、該微粒子の融点以上の温度で加熱し、撥水性
微粒子を、部分的に活性炭表面に融着せしめるこ
とを特徴とするガス拡散電極の製造方法。1 Activated carbon or activated carbon that has adsorbed a catalyst and a water-repellent fine particle dispersion are mixed under reduced pressure, dried, and heated at a temperature higher than the melting point of the fine particles, so that the water-repellent fine particles are partially fused to the surface of the activated carbon. A method for manufacturing a gas diffusion electrode, characterized by dressing the gas diffusion electrode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59153189A JPS6158166A (en) | 1984-07-25 | 1984-07-25 | Manufacture of gas diffusion electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59153189A JPS6158166A (en) | 1984-07-25 | 1984-07-25 | Manufacture of gas diffusion electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6158166A JPS6158166A (en) | 1986-03-25 |
| JPH0326909B2 true JPH0326909B2 (en) | 1991-04-12 |
Family
ID=15556990
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59153189A Granted JPS6158166A (en) | 1984-07-25 | 1984-07-25 | Manufacture of gas diffusion electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6158166A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2017076538A (en) * | 2015-10-15 | 2017-04-20 | Fdk株式会社 | Method for manufacturing air electrode of air secondary battery, and air-hydrogen secondary battery |
-
1984
- 1984-07-25 JP JP59153189A patent/JPS6158166A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6158166A (en) | 1986-03-25 |
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