JPS6318302B2 - - Google Patents
Info
- Publication number
- JPS6318302B2 JPS6318302B2 JP55181393A JP18139380A JPS6318302B2 JP S6318302 B2 JPS6318302 B2 JP S6318302B2 JP 55181393 A JP55181393 A JP 55181393A JP 18139380 A JP18139380 A JP 18139380A JP S6318302 B2 JPS6318302 B2 JP S6318302B2
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- electrode
- air
- polytetrafluoroethylene
- activated carbon
- 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
Links
- 239000001301 oxygen Substances 0.000 claims description 33
- 229910052760 oxygen Inorganic materials 0.000 claims description 33
- -1 perfluoro compound Chemical class 0.000 claims description 33
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 32
- 238000006722 reduction reaction Methods 0.000 claims description 22
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 12
- 229910001882 dioxygen Inorganic materials 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 8
- 150000002894 organic compounds Chemical class 0.000 claims description 8
- 230000003197 catalytic effect Effects 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 36
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 33
- 239000004810 polytetrafluoroethylene Substances 0.000 description 33
- 239000003054 catalyst Substances 0.000 description 14
- 239000011230 binding agent Substances 0.000 description 12
- 239000000843 powder Substances 0.000 description 12
- MPMSMUBQXQALQI-UHFFFAOYSA-N cobalt phthalocyanine Chemical compound [Co+2].C12=CC=CC=C2C(N=C2[N-]C(C3=CC=CC=C32)=N2)=NC1=NC([C]1C=CC=CC1=1)=NC=1N=C1[C]3C=CC=CC3=C2[N-]1 MPMSMUBQXQALQI-UHFFFAOYSA-N 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 11
- 229950011087 perflunafene Drugs 0.000 description 11
- UWEYRJFJVCLAGH-IJWZVTFUSA-N perfluorodecalin Chemical compound FC1(F)C(F)(F)C(F)(F)C(F)(F)[C@@]2(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)[C@@]21F UWEYRJFJVCLAGH-IJWZVTFUSA-N 0.000 description 11
- 238000000034 method Methods 0.000 description 10
- 239000005871 repellent Substances 0.000 description 10
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 9
- 239000010410 layer Substances 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- 239000011148 porous material Substances 0.000 description 8
- 239000010409 thin film Substances 0.000 description 8
- 229910052725 zinc Inorganic materials 0.000 description 8
- 239000011701 zinc Substances 0.000 description 8
- 239000003792 electrolyte Substances 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- NVJHHSJKESILSZ-UHFFFAOYSA-N [Co].N1C(C=C2N=C(C=C3NC(=C4)C=C3)C=C2)=CC=C1C=C1C=CC4=N1 Chemical compound [Co].N1C(C=C2N=C(C=C3NC(=C4)C=C3)C=C2)=CC=C1C=C1C=CC4=N1 NVJHHSJKESILSZ-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 229920000840 ethylene tetrafluoroethylene copolymer Polymers 0.000 description 6
- 239000000539 dimer Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- 239000002131 composite material Substances 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910052759 nickel Inorganic materials 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- KMHSUNDEGHRBNV-UHFFFAOYSA-N 2,4-dichloropyrimidine-5-carbonitrile Chemical compound ClC1=NC=C(C#N)C(Cl)=N1 KMHSUNDEGHRBNV-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000010408 film Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910000000 metal hydroxide Inorganic materials 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 150000004706 metal oxides Chemical class 0.000 description 3
- 239000004745 nonwoven fabric Substances 0.000 description 3
- 150000004032 porphyrins Chemical class 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 239000008280 blood Substances 0.000 description 2
- 210000004369 blood Anatomy 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000005660 hydrophilic surface Effects 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- RVZRBWKZFJCCIB-UHFFFAOYSA-N perfluorotributylamine Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)N(C(F)(F)C(F)(F)C(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F RVZRBWKZFJCCIB-UHFFFAOYSA-N 0.000 description 2
- JAJLKEVKNDUJBG-UHFFFAOYSA-N perfluorotripropylamine Chemical compound FC(F)(F)C(F)(F)C(F)(F)N(C(F)(F)C(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)F JAJLKEVKNDUJBG-UHFFFAOYSA-N 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 230000002940 repellent Effects 0.000 description 2
- CPRMKOQKXYSDML-UHFFFAOYSA-M rubidium hydroxide Chemical compound [OH-].[Rb+] CPRMKOQKXYSDML-UHFFFAOYSA-M 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- NOCLWIPRQIWFMR-UHFFFAOYSA-N 1,1,1,2,3,3-hexafluoro-2-[1,1,2,3,3,3-hexafluoro-2-[1,1,2,3,3,3-hexafluoro-2-(1,1,2,2,3,3,3-heptafluoropropoxy)propoxy]propoxy]-3-(1,2,2,2-tetrafluoroethoxy)propane Chemical compound FC(F)(F)C(F)OC(F)(F)C(F)(C(F)(F)F)OC(F)(F)C(F)(C(F)(F)F)OC(F)(F)C(F)(C(F)(F)F)OC(F)(F)C(F)(F)C(F)(F)F NOCLWIPRQIWFMR-UHFFFAOYSA-N 0.000 description 1
- LWRNQOBXRHWPGE-UHFFFAOYSA-N 1,1,2,2,3,3,4,4,4a,5,5,6,6,7,7,8,8a-heptadecafluoro-8-(trifluoromethyl)naphthalene Chemical compound FC1(F)C(F)(F)C(F)(F)C(F)(F)C2(F)C(C(F)(F)F)(F)C(F)(F)C(F)(F)C(F)(F)C21F LWRNQOBXRHWPGE-UHFFFAOYSA-N 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- ISOVJOUTLMVMKB-UHFFFAOYSA-N ClC(Cl)(Cl)Cl.FC1(F)C(F)(F)C(F)(F)C(F)(F)C2(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C21F Chemical compound ClC(Cl)(Cl)Cl.FC1(F)C(F)(F)C(F)(F)C(F)(F)C2(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C21F ISOVJOUTLMVMKB-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 102000001554 Hemoglobins Human genes 0.000 description 1
- 108010054147 Hemoglobins Proteins 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- ITFCTBFBEKRKDC-UHFFFAOYSA-N [O].OC Chemical compound [O].OC ITFCTBFBEKRKDC-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000012790 adhesive layer Substances 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910021383 artificial graphite Inorganic materials 0.000 description 1
- 229910052792 caesium Inorganic materials 0.000 description 1
- TVFDJXOCXUVLDH-UHFFFAOYSA-N caesium atom Chemical compound [Cs] TVFDJXOCXUVLDH-UHFFFAOYSA-N 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GSOLWAFGMNOBSY-UHFFFAOYSA-N cobalt Chemical compound [Co][Co][Co][Co][Co][Co][Co][Co] GSOLWAFGMNOBSY-UHFFFAOYSA-N 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011245 gel electrolyte Substances 0.000 description 1
- 239000003349 gelling agent Substances 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- QLOAVXSYZAJECW-UHFFFAOYSA-N methane;molecular fluorine Chemical group C.FF QLOAVXSYZAJECW-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 1
- 229950008618 perfluamine Drugs 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- UONOETXJSWQNOL-UHFFFAOYSA-N tungsten carbide Chemical compound [W+]#[C-] UONOETXJSWQNOL-UHFFFAOYSA-N 0.000 description 1
- CMPGARWFYBADJI-UHFFFAOYSA-L tungstic acid Chemical compound O[W](O)(=O)=O CMPGARWFYBADJI-UHFFFAOYSA-L 0.000 description 1
- 238000009736 wetting 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
- H01M4/96—Carbon-based electrodes
-
- 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
- H01M4/90—Selection of catalytic material
- H01M4/9008—Organic or organo-metallic compounds
-
- 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)
- Materials Engineering (AREA)
- Inert Electrodes (AREA)
Description
本発明は、水素−酸素、メタノール−酸素など
の燃料電池、空気−亜鉛、空気−鉄などの金属空
気電池、及び酸素センサ用に適した空気電極(酸
素極)の改良に係るものである。
従来から、各種の燃料電池、空気−亜鉛を始め
とする金属−空気電池、ガルバニ型の酸素センサ
などの空気極には、ガス拡散電極が用いられて来
た。このガス拡散電極は、初期には厚型の均一多
孔性電極が多く用いられてきたが、現在では薄く
てしかも耐漏液性を満足するために、酸素ガスの
電気化学的還元反応を行なわしめる電極本体と撥
水性層とを一体化した二重電極が用いられるよう
になつて来た。
この前記空気電極は以下の如く構成されてい
る。まず、撥水性層としては、ポリテトラフロロ
エチレン、ポリテトラフロロエチレン−ヘキサフ
ロロプロピレン共重合体、ポリエチレン−テトラ
フロロエチレン共重合体等のフツ素樹脂やポリプ
ロピレン等を用い、たとえば0.2〜40μ粒径の粉末
の焼結体、繊維を加熱処理して不織布化した紙状
のもの、同じく繊維布状にしたもの、粉末の一部
をフツ化黒鉛に置きかえたもの、微粉末を増孔
剤・潤滑油などと共にロール加圧した後、加熱処
理をしたフイルム状のもの、あるいはロール加圧
後熱処理をしないフイルム状のもの等の多孔体が
用いられてきた。また、特に漏液が許されない場
合、例えば水中の溶存酸素ガス濃度検出に用いら
れるガルバニ型酸素センサの空気電極には、薄い
耐電解液性・ガス透過性の無孔のフイルムがガス
側に用いられてきた。これらの撥水性層又はガス
透過膜と電極本体である多孔質電極とを加圧ある
いは接着によつて一体化したり、これら撥水性層
上に電極本体構成材料を塗着する事により空気電
極が構成されていた。
この場合の電極本体は、酸素還元過電圧の低い
ニツケルタングステン酸、パラジウム・コバルト
で被覆された炭化タングステン、ニツケル、銀、
白金、パラジウム等の触媒を担持させた活性炭粉
末に、ポリテトラフロロエチレン等を結合剤とし
て、金属多孔質体、カーボン多孔質体、カーボン
繊維不織布等と一体化する事により形成される。
しかしながら、従来の空気電極は例えば薄型の
空気/亜鉛電池の様に、薄くて完全に漏液がな
く、しかも重負荷放電が要求される用途において
は、なお問題を有する。
さて、上記電極本体における酸素ガスの電気化
学的還元反応は、大気中から拡散した空気の気
相、電極本体の固相、および電解液の液相からな
る微視的3相界面において生ずる。この反応を加
速して、重負荷放電を可能にするには、(1)微視的
3相界面におりる酸素ガス濃度(分圧)を高くす
る、(2)酸素ガスの電気化学的還元反応速度を大き
くする、が考慮されねばならない。(2)に関して
は、従来より電極本体に担持させる酸素ガス還元
触媒が多数検討されているが、(1)については、耐
漏液性を考慮しかつ大気中からの空気の拡散を良
好にする目的で、撥水性層としてフツ素樹脂粉末
を焼結した得た多孔体を用いる、薄いガス透過性
の無孔のフイルムをガス側に設ける等が提案され
ているだけである。
しかしながら、撥水層としてフツ素樹脂粉末を
焼結して得た多孔体を用いた場合、約20mA/cm2
程度というかなり重負荷の連続放電を行う事がで
きるが、その厚みは0.125〜0.50mm程度が必要で
あり、又孔径が完全に揃つておらず大きな孔径の
孔が存在する事から、空気電極の対極での体積膨
張等によつて電池内圧上昇を生ずると、特に密閉
型の場合は漏液を引き起す場合もある。一方、漏
液を防止すするために薄いガス透過性の無孔のフ
イルムを接着剤等を用いてガス側に設けた空気電
極においては、完全に漏液を防止でき、また約
12.5μm程度まで厚みを薄くする事も可能である
が、この際には10mA/cm2以上の大電流で連続し
て放電を行うのは非常に困難となる。
本発明は、上記の従来の空気電極の欠点に鑑
み、薄く、重負荷放電が可能で、かつ漏液をより
完全に防止できる様な空気電極を提供する事を目
的とする。
本発明は、空気電極の電極本体中に、耐漏液性
に優れ50mA/cm2以上の連続放電が可能なよう
に、酸素溶解能を有した液状パーフロロ化合物を
鉄フタロシアニン、コバルトフタロシアニン、コ
バルトポルフイリンの2量体等の有機化合物から
成る酸素還元触媒と共に担持させることにより、
従来の欠点を解決して、薄くて重負荷放電が可能
であり、さらに、耐漏液性の優れた空気電極を提
供するものである。
なお、本発明において用いられるパーフロロ化
合物は、その分子量が10000未満特に1000以下の
低分子化合物であることが好ましい。これは分子
量が10000以上になると酸素溶解能が低下し酸素
を溶かしにくくなるからである。この望ましいパ
ーフロロ化合物として具体的には、パーフロロト
リ−n−ブチルアミン(FC−43)、パーフロロト
リプロピルアミン(FTPA)、パーフロロデカリ
ン(FDC)、パーフロロメチルデカリン
(FMD)、パーフロリネイテイドエーテル
(Freon E4)等を用いることができる。これらの
パーフロロ化合物は、酸素溶解能が大きい(約
40vol%、血液の酸素溶解能は約22vol%)と共
に、酸素の授受速度も14〜26msecと速く(血液
中のヘモグロビンの場合は90msec程度)ほとん
ど瞬間的に高なわれ、しかも可逆的である。この
特性のため、酸素溶解能を有した液状パーフロロ
化合物を従来からの有機化合物から成る酸素還元
触媒と空気電極内に於て共存させることにより、
触媒の効果を一層顕著なものとし、しいては、該
電極の大電流放電を容易ならしめるものである。
なお、上記パーフロロ化合物の含有量は、その
添加効果を充分発揮する為には0.1〜1wt%とする
事が好ましい。
上記のごとく、活性炭、及び有機化合物から成
る酸素還元触媒の表面に酸素溶解能が大きいパー
フロロ化合物を担持させることにより、酸素ガス
の電気化学的還元反応が起こる活性炭、および、
コバルトフタロシアニン等の有機化合物から成る
酸素還元触媒の表面における酸素ガス濃度を増大
させ、重負荷放電が可能であると共に、撥水性、
耐電解液性を向上させることにより耐漏液性能が
向上し、寿命の長い空気電極を提供することがで
きる。
また、特に、有機化合物から成る酸素還元触媒
として、金属、ポルフイリンの2量体を選択した
場合においては通常の酸素還元触媒に見られるよ
うな2電子還元が起こるのとは異なり、一きよに
4電子還元が起こる。そのため、該触媒をパーフ
ロロ化合物と共存させて選択した場合には酸素の
還元反応が円滑に進行し、その表面における酸素
ガス授受速度を本発明による酸素溶解能を有した
液状パーフロロ化合物を用いて、増大させた時に
は、その触媒効果を著しく向上することができる
ものである。本発明に使用する金属ポルフイリン
の構造式の例を第1図及第2図に示す。
なおこれらの各種金属ポルフイリンの2量体の
含有量は、活性炭重量に対し1wt%未満では触媒
活性が低くなり、また10wt%を越えると触媒能
力と酸素吸着能力とが充分発揮されない為、この
範囲とする事が好ましい。また、カーボンやニツ
ケルなどの粉末を主成分として作成される空気電
極においては、これらの粉末にPTFEの粉末ある
いは懸濁液を混合し、ついで加圧成形し、さらに
必要に応じ200〜300℃で加熱する方法、いわゆる
テフロン結着法が知られており、この方法により
比較的良好な空気電極が作製できる。しかしなが
ら、電極内にはまだ親水性の面がかなり露出して
おり、この部分を通して電解液が電極内に徐々に
浸透し、この“ぬれ”によつて電極内へのガスの
拡散が充分に行なわれ難くなり、電極の重負荷特
性の安定性が阻害される。この原因として、以下
の様なことが考えられる。結着剤として用いられ
るPTFEは、水等の溶媒に対してきわめて難溶で
あるため、PTFEの粉末又は懸濁液が用いられて
いる。しかしこの懸濁液中のPTFEの粒径の最小
は0.2μm程度で、これより粒径の小さい懸濁液を
得ることは困難である。そのため、活性炭や多孔
質焼結体の空隙孔の径がPTFEの粒径に比べ大き
くない限り、PTFE粒子の空隙内への進入は期待
できない。したがつて、電極内には親水性の面が
残ることとなる。そこで、PTFE粒子が空隙孔の
内部へ深く進入できるように、多孔質焼結体の空
隙孔の孔径をPTFEの懸濁粒子の径よりも大きく
する方法が提案されている。しかし、このように
電極の空隙孔の孔径を大きくすると、起電反応に
有効な3相界面の形状は粗大化し、表面積が減少
して大電流をとり出すことができなくなる。まし
て活性炭の空隙等の微細孔内への進入は望めな
い。
一方、本発明によれば、用いられる酸素溶解能
を有した液状パーフロロ化合物は、PTFEよりも
低分子量であるため、活性炭の微細孔内へも容易
に進入することができ、撥水効果を増大すること
ができる。
上記のように、本発明によれば、従来の酸素還
元触媒として作用する有機化合物と酸素溶解能を
有した液状パーフロロ化合物とを共存させて電極
内に担持させることにより、酸素溶解能を高め、
電極内の酸素濃度を増大させ得るとともに、撥水
効果をも付与することができ、耐漏液性に優れ、
かつ、重負荷放電が可能な空気電極が構成でき
る。
また、さらに電極本体として孔径が0.1〜10μm
の多孔質体を用いる事により一層優れた特性のも
のが得られる。つまり酸素の還元生成物イオンの
除去速度が速くなり50mA/cm2以上の電流を容易
に取り出せる上、撥水性層が一層均一なものとな
り機械的強度も向上する。
本発明に係る空気電極を用いる場合は、実用上
電極本体中又は電極本体の電解液側に酸素の酸化
還元電位より0.4V以内卑な電位を有する金属酸
化物又は水酸化物を用いる事により、断続的に放
電を行う際、酸素の電気化学的な還元以外に、電
極構成要素自体の電気化学的還元によつて、瞬間
的な大電流供給が可能となる。なお、該金属酸化
物、又は該水酸化物は、軽負荷放電中又は開路時
には、ローカルセルアクシヨンで酸素ガスによつ
て酸化され、もとの酸化状態に復帰させる事がで
きる。
なお、酸素の酸化還元電位より0.4V以内卑な
電位を有する金属酸化物又は水酸化物としては
Ag3O、MnO2、CO2O3、PbO2、各種ペロプスカ
イト型酸化物、スピネル型酸化物を用いる事がで
きる。
以下、実施例によつて本発明を詳細に説明す
る。
実施例 1
コバルトフタロシアニンのピリジン溶液中に活
性炭を懸濁させることにより、10重量%のコバル
トフタロシアニンを添加した活性炭粉末に0.1〜
5%のパーフロロデカリン四塩化炭素溶液で吸着
処理を行ない、0.5重量%のパーフロロデカリン
を添加しこれを触媒粉末とし、これに結着剤とし
て10〜20重量%のポリテトラフロロエチレンをデ
イスパージヨンの形態で混合、混練し、展開し
て、シート状に形成し、集電体として使用するニ
ツケル金網に圧着して、厚さ0.7mmの電極本体を
作成した。これに厚さ6μmの撥水性層としての
ポリテトラフロロエチレン(PTFE)/熱融着性
接着層としてのエチレン−テトラフロロエチレン
共重合体の積層体からなる複合薄膜を240℃で熱
融着することにより、全体で約0.7mmの厚みの空
気電極とした。
実施例 2
水溶性スルフオン化コバルトフタロシアニンの
0.05M硫酸溶液中に活性炭を懸濁させることによ
り10重量%のスルフオン化コバルトフタロシアニ
ンを含有した活性炭粉末を窒素雰囲気中で650℃
1時間熱処理を行なつた後、実施例1と全く同じ
方法により0.5重量%のパーフロロデカリンを吸
着させ10〜20重量%のポリテトラフロロエチレン
を結着剤とし厚さ6μmのポリテトラフロロエチ
レン/エチレン−テトラフロロエチレン共重合体
の積層体からなる複合薄膜を熱融着することによ
り約0.7mmの厚さの空気電極を作成した。
実施例 3
鉄フタロシアニンの濃硫酸溶液中に活性炭を懸
濁させ、これを0℃に急冷することにより約10重
量%の鉄フタロシアニンを添加した活性炭粉末を
用い、実施例1と全く同じ方法により、0.5重量
%のパーフロロデカリンを吸着させ、ポリテトラ
フロロエチレンを結着剤とし、ポリテトラフロロ
エチレン/エチレン−テトラフロロエチレン共重
合体の複合薄膜を熱融着させ約0.7mmの厚さの空
気電極を作成した。
実施例 4
コバルトポルフイリン2量体のジクロロメタン
溶液中に活性炭を懸濁させることにより5重量%
のコバルトポルフイリン2量体を添加した活性炭
を用い、実施例1と全く同じ方法で0.5重量%の
パーフロロデカリンを吸着させポリテトラフロロ
エチレンを結着剤とし、ポリテトラフロロエチレ
ン/エチレン−テトラフロロエチレン共重合体の
複合薄膜を熱融着させ、約0.7mmの厚さの空気極
を作成した。なお本実施例に使用したコバルトポ
ルフイリンの2量体は図1においてM=M′=C0
の構造のものを使用した。
比較例 1
塩化パラジウムの水溶液に活性炭粉末を懸濁さ
せ、ホルマリンで還元した触媒付活性粉末を、10
〜15%のポリテトラフロロエチレン樹脂
(PTFE)デイスパージヨンで防水処理をほどこ
し、防水解液粉末とし、これに結着剤として
PTFEを混合してシートとなし、ニツケルネツト
に圧着して厚さ0.6mmの空気電極本体とした。次
に、人造黒鉛粉末に、PTFE樹脂デイスパージヨ
ンを混合して加熱処理をし、防水黒鉛粉末とし、
これに結着剤としてPTFEを加えてシートとし、
これを上記電極本体に重ねて圧着し、加熱処理を
する事により全体で1.0mmの厚みの2重層構造の
空気電極とした。
比較例 2
実施例1と全く同様の方法で10重量%のコバル
トフタロシアニンを添加した活性炭粉末にパーフ
ロロデカリンを吸着させずにポリテトラフロロエ
チレンを結着剤としてシート状に成形し、厚さ
0.7mmの電極本体を作成した。この電極本体にポ
リテトラフロロエチレン/エチレン−テトラフロ
ロエチレン共重合体薄膜を熱融着させ空気電極を
作成した。
比較例 3
実施例4と全く同様にして5重量%のコバルト
ポルフイリン2量体を添加した活性炭にパーフロ
ロデカリンを吸着されずに用い、ポリテトラフロ
ロエチレンを結着剤としてシート状に成形し、電
極本体を作成した。この電極本体にポリテトラフ
ロロエチレン/エチレン・テトラフロロエチレン
共重合体薄膜を熱融着させ空気電極を作成した。
なお本比較例に使用したコバルトポルフイリンの
2量体は図1においてM=M′=C0の構造式を有
するものを使用した。
上記の実施例、比較例による空気電極の性能を
試るために、熱量比で3%の水銀でアマルガム化
した60〜150メツシユバスの亜鉛粉末を、水酸化
ナトリウム溶液中にゲル化剤を分散させて調製し
たゲル状電解液中に分散させた亜鉛極を対極と
し、ポリアミドの不織布をセパレータとした空気
−亜鉛電池を組み立てた。これらの空気−亜鉛電
池を25℃空気中で16時間放置した後、各種の電流
で5分間放電し5分後の端子電圧が1.0V以下と
なる電流値を測定した。又、温度45℃、相対湿度
90%で上記空気−亜鉛電池を保存し、漏液状態を
観察した。
以下にその結果を示す。
The present invention relates to improvements in air electrodes (oxygen electrodes) suitable for fuel cells such as hydrogen-oxygen and methanol-oxygen, metal-air batteries such as air-zinc and air-iron, and oxygen sensors. Conventionally, gas diffusion electrodes have been used as air electrodes in various fuel cells, metal-air batteries including air-zinc batteries, galvanic oxygen sensors, and the like. In the early days, thick uniformly porous electrodes were often used as gas diffusion electrodes, but in order to be thinner and have leakage resistance, electrodes that perform an electrochemical reduction reaction of oxygen gas are now used. Dual electrodes in which the main body and the water-repellent layer are integrated have come into use. This air electrode is constructed as follows. First, for the water-repellent layer, a fluororesin or polypropylene such as polytetrafluoroethylene, polytetrafluoroethylene-hexafluoropropylene copolymer, polyethylene-tetrafluoroethylene copolymer, etc. is used, and the particle size is, for example, 0.2 to 40μ. A sintered body of powder, a paper-like thing made by heat-treating the fibers to make it into a non-woven fabric, a thing made into the same fiber cloth-like form, a thing where a part of the powder is replaced with graphite fluoride, a fine powder used as a pore-forming agent and a lubricant. Porous bodies have been used, such as film-like materials that are subjected to heat treatment after being roll-pressed with oil or the like, or film-like materials that are not heat-treated after being roll-pressed. In addition, in cases where liquid leakage is not allowed, for example, a thin electrolyte-resistant, gas-permeable, non-porous film is used on the gas side of the air electrode of a galvanic oxygen sensor used to detect the concentration of dissolved oxygen gas in water. I've been exposed to it. An air electrode is constructed by integrating these water-repellent layers or gas-permeable membranes with the porous electrode that is the electrode body by applying pressure or adhesion, or by coating the electrode body constituent materials on these water-repellent layers. It had been. In this case, the electrode body is made of nickel tungstic acid with low oxygen reduction overpotential, tungsten carbide coated with palladium/cobalt, nickel, silver, etc.
It is formed by integrating activated carbon powder supporting a catalyst such as platinum or palladium with a metal porous body, a carbon porous body, a carbon fiber nonwoven fabric, etc. using polytetrafluoroethylene or the like as a binder. However, conventional air electrodes still have problems in applications where they are thin and completely leak-proof, such as thin air/zinc batteries, and yet require heavy load discharge. The electrochemical reduction reaction of oxygen gas in the electrode body occurs at a microscopic three-phase interface consisting of the gas phase of air diffused from the atmosphere, the solid phase of the electrode body, and the liquid phase of the electrolyte. To accelerate this reaction and enable heavy load discharge, (1) increase the oxygen gas concentration (partial pressure) at the microscopic three-phase interface, (2) electrochemical reduction of oxygen gas. Consideration must be given to increasing the reaction rate. Regarding (2), many oxygen gas reduction catalysts supported on the electrode body have been studied, but regarding (1), the purpose is to consider leakage resistance and improve the diffusion of air from the atmosphere. However, it has only been proposed to use a porous body obtained by sintering fluororesin powder as a water-repellent layer, and to provide a thin gas-permeable non-porous film on the gas side. However, when a porous body obtained by sintering fluorine resin powder is used as the water-repellent layer, the power consumption is approximately 20 mA/cm 2
It is possible to carry out continuous discharge with a fairly heavy load of approximately 1.5 mm, but the thickness needs to be approximately 0.125 to 0.50 mm, and the pore diameters are not perfectly aligned and there are large pores, so it is difficult to use an air electrode. If the internal pressure of the battery increases due to volume expansion at the counter electrode, it may cause leakage, especially in the case of a sealed type battery. On the other hand, an air electrode in which a thin, gas-permeable, non-porous film is attached to the gas side using an adhesive or the like to prevent liquid leakage can completely prevent liquid leakage, and approximately
Although it is possible to reduce the thickness to about 12.5 μm, in this case it would be extremely difficult to discharge continuously at a large current of 10 mA/cm 2 or more. SUMMARY OF THE INVENTION In view of the above-mentioned drawbacks of the conventional air electrode, an object of the present invention is to provide an air electrode that is thin, capable of heavy load discharge, and more completely prevents leakage. The present invention incorporates iron phthalocyanine, cobalt phthalocyanine, and cobalt porphyrin into the electrode body of an air electrode, in order to have excellent leakage resistance and enable continuous discharge of 50 mA/cm 2 or more. By supporting it together with an oxygen reduction catalyst consisting of an organic compound such as a dimer of
The present invention solves the conventional drawbacks and provides an air electrode that is thin, capable of heavy load discharge, and has excellent leakage resistance. The perfluoro compound used in the present invention is preferably a low-molecular compound with a molecular weight of less than 10,000, particularly 1,000 or less. This is because when the molecular weight exceeds 10,000, the oxygen dissolving ability decreases and it becomes difficult to dissolve oxygen. These desirable perfluorinated compounds include perfluorotri-n-butylamine (FC-43), perfluorotripropylamine (FTPA), perfluorodecalin (FDC), perfluoromethyldecalin (FMD), perfluorinated ether ( Freon E 4 ) etc. can be used. These perfluoro compounds have a large oxygen solubility (approximately
40 vol%, the oxygen solubility of blood is about 22 vol%), and the rate of oxygen transfer is as fast as 14 to 26 msec (about 90 msec for hemoglobin in the blood), which increases almost instantaneously, and is reversible. Because of this characteristic, by coexisting a liquid perfluoro compound with oxygen dissolving ability with a conventional oxygen reduction catalyst made of an organic compound in the air electrode,
This makes the effect of the catalyst even more remarkable, and thus facilitates the discharge of a large current from the electrode. In addition, the content of the above-mentioned perfluoro compound is preferably 0.1 to 1 wt% in order to fully exhibit the effect of its addition. As mentioned above, an activated carbon in which an electrochemical reduction reaction of oxygen gas occurs by supporting a perfluoro compound having a large oxygen dissolving ability on the surface of an oxygen reduction catalyst made of activated carbon and an organic compound, and
By increasing the oxygen gas concentration on the surface of the oxygen reduction catalyst made of organic compounds such as cobalt phthalocyanine, it is possible to perform heavy load discharge, and also has water repellency.
By improving electrolyte resistance, leakage resistance is improved, and an air electrode with a long life can be provided. Furthermore, in particular, when a dimer of metal or porphyrin is selected as an oxygen reduction catalyst consisting of an organic compound, unlike the two-electron reduction that occurs in ordinary oxygen reduction catalysts, four-electron reduction occurs at once. Electron reduction occurs. Therefore, when the catalyst is selected in coexistence with a perfluoro compound, the oxygen reduction reaction proceeds smoothly, and the oxygen gas exchange rate on the surface can be adjusted by using the liquid perfluoro compound having oxygen dissolving ability according to the present invention. When increased, the catalytic effect can be significantly improved. Examples of the structural formulas of metal porphyrins used in the present invention are shown in FIGS. 1 and 2. It should be noted that if the content of dimers of these various metal porphyrins is less than 1wt% based on the weight of activated carbon, the catalytic activity will be low, and if it exceeds 10wt%, the catalytic ability and oxygen adsorption ability will not be fully demonstrated, so it is recommended that the content be within this range. It is preferable to do so. In addition, for air electrodes made mainly of powders such as carbon and nickel, these powders are mixed with PTFE powder or suspension, then pressure molded, and further heated at 200 to 300℃ as necessary. A heating method, the so-called Teflon bonding method, is known, and a relatively good air electrode can be produced by this method. However, there is still a large exposed hydrophilic surface within the electrode, through which the electrolyte gradually penetrates into the electrode, and this "wetting" is sufficient for gas diffusion into the electrode. As a result, the stability of the heavy load characteristics of the electrode is impaired. Possible causes of this are as follows. PTFE used as a binder is extremely poorly soluble in solvents such as water, so PTFE powder or suspension is used. However, the minimum particle size of PTFE in this suspension is about 0.2 μm, and it is difficult to obtain a suspension with a particle size smaller than this. Therefore, unless the diameter of the pores in the activated carbon or porous sintered body is larger than the particle size of PTFE, PTFE particles cannot be expected to enter the pores. Therefore, a hydrophilic surface remains within the electrode. Therefore, a method has been proposed in which the pore diameter of the porous sintered body is made larger than the diameter of the suspended PTFE particles so that the PTFE particles can deeply penetrate into the pores. However, when the pore diameter of the electrode is increased in this manner, the shape of the three-phase interface effective for electromotive reaction becomes coarser, the surface area decreases, and a large current cannot be extracted. Furthermore, it cannot be expected to enter into micropores such as voids of activated carbon. On the other hand, according to the present invention, the liquid perfluoro compound with oxygen dissolution ability used has a lower molecular weight than PTFE, so it can easily enter into the micropores of activated carbon, increasing the water repellent effect. can do. As described above, according to the present invention, an organic compound that acts as a conventional oxygen reduction catalyst and a liquid perfluoro compound having an oxygen dissolving ability are made to coexist and supported in an electrode, thereby increasing the oxygen dissolving ability.
In addition to increasing the oxygen concentration within the electrode, it can also provide a water repellent effect, and has excellent leakage resistance.
Moreover, an air electrode capable of heavy load discharge can be constructed. In addition, the electrode body has a pore diameter of 0.1 to 10 μm.
By using a porous body, even more excellent properties can be obtained. In other words, the rate of removal of oxygen reduction product ions becomes faster, and a current of 50 mA/cm 2 or more can be easily obtained, and the water-repellent layer becomes more uniform, resulting in improved mechanical strength. When using the air electrode according to the present invention, in practice, by using a metal oxide or hydroxide in the electrode body or on the electrolyte side of the electrode body, which has a potential within 0.4 V less base than the redox potential of oxygen. When discharging intermittently, in addition to the electrochemical reduction of oxygen, the electrochemical reduction of the electrode components themselves makes it possible to instantaneously supply a large current. Note that the metal oxide or hydroxide is oxidized by oxygen gas in the local cell action during light load discharge or when the circuit is opened, and can be returned to the original oxidized state. In addition, metal oxides or hydroxides that have a potential less than 0.4 V less than the redox potential of oxygen include:
Ag 3 O, MnO 2 , CO 2 O 3 , PbO 2 , various perovskite-type oxides, and spinel-type oxides can be used. Hereinafter, the present invention will be explained in detail with reference to Examples. Example 1 By suspending activated carbon in a pyridine solution of cobalt phthalocyanine, activated carbon powder to which 10% by weight of cobalt phthalocyanine was added was
Adsorption treatment is performed with a 5% perfluorodecalin carbon tetrachloride solution, 0.5% by weight of perfluorodecalin is added to form a catalyst powder, and 10 to 20% by weight of polytetrafluoroethylene is added as a binder. The mixture was mixed in the form of a sparge, kneaded, spread, formed into a sheet, and pressed onto a nickel wire gauze used as a current collector to create an electrode body with a thickness of 0.7 mm. To this, a composite thin film consisting of a laminate of polytetrafluoroethylene (PTFE) as a water-repellent layer with a thickness of 6 μm and ethylene-tetrafluoroethylene copolymer as a heat-adhesive layer is heat-sealed at 240°C. As a result, the total thickness of the air electrode was approximately 0.7 mm. Example 2 Water-soluble sulfonated cobalt phthalocyanine
Activated carbon powder containing 10% by weight of sulfonated cobalt phthalocyanine was prepared by suspending the activated carbon in a 0.05M sulfuric acid solution at 650°C in a nitrogen atmosphere.
After heat treatment for 1 hour, 0.5% by weight of perfluorodecalin was adsorbed using the same method as in Example 1, and 6 μm thick polytetrafluoroethylene was formed using 10 to 20% by weight of polytetrafluoroethylene as a binder. An air electrode with a thickness of approximately 0.7 mm was prepared by heat-sealing a composite thin film consisting of a laminate of /ethylene-tetrafluoroethylene copolymer. Example 3 Using activated carbon powder to which approximately 10% by weight of iron phthalocyanine was added by suspending activated carbon in a concentrated sulfuric acid solution of iron phthalocyanine and rapidly cooling it to 0°C, the same method as in Example 1 was carried out. 0.5% by weight of perfluorodecalin is adsorbed, polytetrafluoroethylene is used as a binder, and a composite thin film of polytetrafluoroethylene/ethylene-tetrafluoroethylene copolymer is heat-sealed to form a layer of air approximately 0.7 mm thick. Created an electrode. Example 4 5% by weight of cobalt porphyrin dimer by suspending activated carbon in dichloromethane solution
Using activated carbon added with cobalt porphyrin dimer, 0.5% by weight of perfluorodecalin was adsorbed in exactly the same manner as in Example 1, polytetrafluoroethylene was used as a binder, and polytetrafluoroethylene/ethylene-tetra An air electrode with a thickness of approximately 0.7 mm was created by heat-sealing a composite thin film of fluoroethylene copolymer. The dimer of cobalt porphyrin used in this example is M=M′=C 0 in FIG.
A structure with the following structure was used. Comparative Example 1 Activated carbon powder was suspended in an aqueous solution of palladium chloride and activated powder with catalyst was reduced with formalin.
Waterproof treatment is applied with ~15% polytetrafluoroethylene resin (PTFE) dispersion to form a waterproof solution powder, and this is used as a binder.
PTFE was mixed into a sheet, which was pressed onto a nickel net to form an air electrode body with a thickness of 0.6 mm. Next, artificial graphite powder is mixed with PTFE resin dispersion and heat treated to make waterproof graphite powder.
PTFE is added as a binder to this to form a sheet.
This was stacked on the electrode body and crimped and heat-treated to form a double-layered air electrode with a total thickness of 1.0 mm. Comparative Example 2 In exactly the same manner as in Example 1, activated carbon powder to which 10% by weight of cobalt phthalocyanine was added was formed into a sheet shape using polytetrafluoroethylene as a binder without adsorbing perfluorodecalin, and the thickness was
A 0.7 mm electrode body was created. A polytetrafluoroethylene/ethylene-tetrafluoroethylene copolymer thin film was heat-sealed to this electrode body to prepare an air electrode. Comparative Example 3 In exactly the same manner as in Example 4, perfluorodecalin was used without being adsorbed on activated carbon to which 5% by weight of cobalt porphyrin dimer was added, and polytetrafluoroethylene was used as a binder to form a sheet into a sheet. , the electrode body was created. A polytetrafluoroethylene/ethylene/tetrafluoroethylene copolymer thin film was heat-sealed to this electrode body to create an air electrode.
The cobalt porphyrin dimer used in this comparative example had the structural formula M=M'=C 0 in FIG. 1. In order to test the performance of the air electrodes according to the above Examples and Comparative Examples, 60 to 150 mesh baths of zinc powder amalgamated with 3% mercury in terms of calorific value were dispersed in a sodium hydroxide solution with a gelling agent. An air-zinc battery was assembled using a zinc electrode dispersed in a gel electrolyte prepared as a counter electrode and a polyamide nonwoven fabric as a separator. These air-zinc batteries were left in the air at 25° C. for 16 hours, then discharged for 5 minutes at various currents, and the current value at which the terminal voltage was 1.0 V or less after 5 minutes was measured. Also, temperature 45℃, relative humidity
The above air-zinc battery was stored at 90% and the state of leakage was observed. The results are shown below.
【表】
上表より明らかなように、本発明方法による空
気電極を用いれば、重負荷放電が可能となり、し
かも漏液性能が向上する。
また、触媒作用を有する有機化合物及びパーフ
ロロ化合物の組合せによる効果を確認するために
以下のような電極を作製した。
比較例 4
実施例1と全く同様の方法を用い、コバルトフ
タロシアニンは吸着させず、0.5重量%のパーフ
ロロデカリンだけを吸着させた活性炭粉末を用い
てポリテトラフロロエチレンを結着剤としてシー
ト状に成形し、厚さ0.7mmの電極本体を作成した。
この電極本体にポリテトラフロロエチレン/エチ
レン−テトラフロロエチレン共重合体薄膜を熱融
着させ空気電極を作成した。
比較例 5
活性炭粉末にはコバルトフタロシアニン及びパ
ーフロロデカリンのどちらも吸着せずに、他は実
施例1と全く同様の方法を用いて、ポリテトラフ
ロロエチレンを結着剤としてシート状に成形し、
厚さ0.7mmの電極本体を作成した。この電極本体
にポリテトラフロロエチレン/エチレン−テトラ
フロロエチレン共重合体薄膜を熱融着させ空気電
極を作製した。
これら比較例4及び5による電極を、実施例1
及び比較例2と同様の条件で測定観察した。その
結果を以下の表2に実施例1及び比較例2も併記
してまとめた。[Table] As is clear from the above table, by using the air electrode according to the method of the present invention, heavy load discharge is possible and the leakage performance is improved. In addition, in order to confirm the effect of the combination of an organic compound having a catalytic action and a perfluoro compound, the following electrode was produced. Comparative Example 4 Using exactly the same method as in Example 1, activated carbon powder on which only 0.5% by weight of perfluorodecalin was adsorbed without adsorbing cobalt phthalocyanine was used to form a sheet using polytetrafluoroethylene as a binder. It was molded to create an electrode body with a thickness of 0.7 mm.
A polytetrafluoroethylene/ethylene-tetrafluoroethylene copolymer thin film was heat-sealed to this electrode body to prepare an air electrode. Comparative Example 5 Activated carbon powder was formed into a sheet using polytetrafluoroethylene as a binder using the same method as in Example 1 except that neither cobalt phthalocyanine nor perfluorodecalin was adsorbed.
An electrode body with a thickness of 0.7 mm was created. A polytetrafluoroethylene/ethylene-tetrafluoroethylene copolymer thin film was heat-sealed to this electrode body to produce an air electrode. The electrodes according to Comparative Examples 4 and 5 were used in Example 1.
Measurements and observations were made under the same conditions as in Comparative Example 2. The results are summarized in Table 2 below along with Example 1 and Comparative Example 2.
【表】
表2からわかるように本発明に係る空気電極
は、コバルトフタロシアニン及びパーフロロデカ
リンをそれぞれ単独に用いた場合に比べてさらに
電流密度の向上がなされている。これはパーフロ
ロデカリンにより酸素ガスがより多く、コバルト
フタロシアニンよりなる触媒の表面に供給される
ことからなされたものである。
なお上記実施例においては水酸化ナトリウムを
電解液とする空気−亜鉛電池を組み立てて、その
性能評価を行つたが、他の電解液、例えば塩化ア
ンモニウムや水酸化カリウムや、水酸化リチウ
ム・水酸化セシウム・水酸化ルビジウム等をこれ
ら溶液に混合した溶液を用いても同様の効果が得
られる事は言うまでもない。又空気−鉄電池にも
用いる事ができる。
以上詳述した如く、本発明方法を用いる事によ
り薄くて重負荷放電が可能で、かつ漏液の起こり
にくい空気電極を容易に得る事ができ工業上利用
価値の大きなものと言える。[Table] As can be seen from Table 2, the current density of the air electrode according to the present invention is further improved compared to the case where cobalt phthalocyanine and perfluorodecalin are used alone. This was done because perfluorodecalin supplies more oxygen gas to the surface of the catalyst made of cobalt phthalocyanine. In the above example, an air-zinc battery using sodium hydroxide as the electrolyte was assembled and its performance was evaluated, but other electrolytes such as ammonium chloride, potassium hydroxide, lithium hydroxide/hydroxide It goes without saying that similar effects can be obtained by using a solution in which cesium, rubidium hydroxide, etc. are mixed with these solutions. It can also be used in air-iron batteries. As detailed above, by using the method of the present invention, it is possible to easily obtain a thin air electrode that is capable of discharging under a heavy load and is less likely to cause leakage, and can therefore be said to have great industrial utility value.
第1図、及び第2図は、本発明の金属ポルフイ
リンの2量体の構造式のうちのある例を示し、実
施例4、および比較例3の場合には第1図の構造
式のものでM=M′=C0の構造のものを使用した。
1 and 2 show examples of the structural formulas of metalloporphyrin dimers of the present invention, and in the case of Example 4 and Comparative Example 3, the structural formulas of FIG. 1 are shown. A structure with M=M′=C 0 was used.
Claims (1)
に、酸素還元反応に対して触媒作用を有する有機
化合物と酸素溶解能を有した液状パーフロロ化合
物とを共存担持させたことを特徴とする空気電
極。1. An air electrode characterized in that an organic compound having a catalytic effect on an oxygen reduction reaction and a liquid perfluoro compound having an oxygen dissolving ability are co-supported in an electrode body that performs electrochemical reduction of oxygen gas. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55181393A JPS57105969A (en) | 1980-12-23 | 1980-12-23 | Air electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55181393A JPS57105969A (en) | 1980-12-23 | 1980-12-23 | Air electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57105969A JPS57105969A (en) | 1982-07-01 |
| JPS6318302B2 true JPS6318302B2 (en) | 1988-04-18 |
Family
ID=16099951
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55181393A Granted JPS57105969A (en) | 1980-12-23 | 1980-12-23 | Air electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57105969A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4635248B2 (en) * | 2004-08-18 | 2011-02-23 | 独立行政法人産業技術総合研究所 | Cathode electrode catalyst for polymer electrolyte fuel cell and production method thereof |
| JP5234534B2 (en) * | 2007-05-24 | 2013-07-10 | 国立大学法人大阪大学 | Method for evaluating performance of battery electrode catalyst comprising N4 chelate-type dimerized metal complex |
-
1980
- 1980-12-23 JP JP55181393A patent/JPS57105969A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57105969A (en) | 1982-07-01 |
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