TW201228081A - Electrodes and production and use thereof - Google Patents

Electrodes and production and use thereof Download PDF

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TW201228081A
TW201228081A TW100121692A TW100121692A TW201228081A TW 201228081 A TW201228081 A TW 201228081A TW 100121692 A TW100121692 A TW 100121692A TW 100121692 A TW100121692 A TW 100121692A TW 201228081 A TW201228081 A TW 201228081A
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range
compound
electrode
group
formula
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Arnd Garsuch
Alexander Panchenko
Andrey Karpov
Rudiger Schmidt
Sabine Huber
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Basf Se
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M12/00Hybrid cells; Manufacture thereof
    • H01M12/04Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M12/00Hybrid cells; Manufacture thereof
    • H01M12/08Hybrid cells; Manufacture thereof composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M12/00Hybrid cells; Manufacture thereof
    • H01M12/04Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
    • H01M12/06Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/8663Selection of inactive substances as ingredients for catalytic active masses, e.g. binders, fillers
    • H01M4/8673Electrically conductive fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9016Oxides, hydroxides or oxygenated metallic salts
    • 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
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/023Porous and characterised by the material
    • H01M8/0234Carbonaceous material
    • 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
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/023Porous and characterised by the material
    • H01M8/0241Composites
    • H01M8/0243Composites in the form of mixtures
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1007Fuel cells with solid electrolytes with both reactants being gaseous or vaporised
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M12/00Hybrid cells; Manufacture thereof
    • H01M12/08Hybrid cells; Manufacture thereof composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
    • H01M12/085Zinc-halogen cells or batteries
    • 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
    • Y02E60/10Energy storage using batteries
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Composite Materials (AREA)
  • Materials Engineering (AREA)
  • Inert Electrodes (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Hybrid Cells (AREA)

Abstract

Electrodes, comprising (A) a solid medium through which gas can diffuse, (B) at least one electrically conductive, carbonaceous material, (C) at least one organic polymer, (D) at least one compound of the general formula (I) M1aM2bM3cM4dHeOf (I) in particulate form, where the variables are each defined as follows: M1 is selected from Mo, W, V, Nb and Sb, M2 is selected from Fe, Ag, Cu, Ni, Mn and lanthanoids, M3 is selected from B, C, N, Al, Si, P and Sn, M4 ist selected from Li, Na, K, Rb, Cs, NH4, Mg, Ca and Sr, a is in the range from 1 to 3, b is in the range from 0.1 to 10, c is in the range from zero to one, d is in the range from zero to one, e is in the range from zero to 5, f is in the range from 1 to 28, and wherein compound of the general formula (I) has a BET surface area in the range from 1 to 300m<SP>2</SP>/g.

Description

201228081 六、發明說明: 【發明所屬之技;術領域】 本發明係關於一種電極,其包含: (A) 氣體可擴散通過之固體介質, (B) 至少一種導電碳質材料, (C) 至少一種有機聚合物, (D) 至少一種呈顆粒形式之通式⑴之化合物 M1aM2bM3cM4dHe〇f (I) 其中該等變數各定義如下: M1 係選自 Mo、W、V、Nb及 Sb, Μ2係選自Fe、Ag、Cu、Ni、Μη及鑭系金屬, M3 係選自 B、C、N、A卜 Si、P及 Sn, M4 係選自 Li、Na ' K、Rb、Cs、NH4、Mg、Ca及 Sr, a 係於1至3之範圍内, b 係於0.1至10之範圍内, C 係於0至1之範圍内, d 係於0至1之範圍内, e 係於0至5之範圍内, f 係於1至28之範圍内, 及其中通式(I)之化合物具有在i至3〇〇 m2/g範圍内之咖表 面積。 丁电犯,例 於金屬-空氣電池組,例如,於鎘-空氣電池组、紹. 池組或鐵-空氣電池組,及尤其於Zn•空氣電池組; 156873.doc 201228081 途。本發明進一步係關於一種製造本發明電化學電池之方 法’及一種製造本發明電極之方法。 【先前技術】 已對習知電化學電池之替代方案研究多年,於習知電化 學電池中,電荷傳輸係於一定程度上經水合質子實施,及 因此最大電壓受到限制。於此方面用於電能之一替代儲存 介質係鋰離子電池組,其中電荷傳輸係藉由非水性溶劑中 之鋰離子確保。然而,許多此類電池組對空氣及水分敏 感,其在最壞情況中會導致有瑕疵的鋰離子電池組自燃。 此外,期望電化學電池具有高能量密度。 藉由金屬-空氣電池組(例如,辞_空氣電池組)提供一種 改進措施。於-常見實施例中,在驗性電解質存在下藉由 大氣氧氣氧化金屬(例如,辞)以形成氧化物或氫氧化物。 斤釋放之此里以電化學方式被利用。此類電池組可藉由還 原放電中所形成之金屬離子而再充電。就此目的而言,已 知將氣體擴散電極(GDE)用作陰極。氣體擴散電極係多孔 r且-有雙功靶作用。金屬_空氣電池組必需應可在放電 期間使大氣氧氣還原成氫氧根離子,及在充電期間使氫氧 根離子氧化成氧氣。就此目的而t,例如,已知曉氣體擴 散電極位於由精細分散碳組成之載體材料上之構造,該載 體材料包含用於催化氧氣還原或氧氣析出&amp;或多㈣ 媒。 此處觸媒之選擇甚為重要。於本文中,描述下列之區 別:純放電觸媒,例如,金屬氧化物,例如,論〇2、 156873.doc 201228081201228081 VI. Description of the Invention: [Technology of Invention] Field of the Invention The present invention relates to an electrode comprising: (A) a solid medium through which a gas can diffuse, (B) at least one conductive carbonaceous material, (C) at least An organic polymer, (D) at least one compound of the formula (1) M1aM2bM3cM4dHe〇f (I) in the form of particles, wherein the variables are each defined as follows: M1 is selected from the group consisting of Mo, W, V, Nb and Sb, and Μ2 is selected From Fe, Ag, Cu, Ni, Μη and lanthanide metals, M3 is selected from B, C, N, A, Si, P and Sn, and M4 is selected from Li, Na'K, Rb, Cs, NH4, Mg , Ca and Sr, a are in the range of 1 to 3, b is in the range of 0.1 to 10, C is in the range of 0 to 1, d is in the range of 0 to 1, and e is in the range of 0 to 1. Within the range of 5, f is in the range of 1 to 28, and the compound of the formula (I) thereof has a coffee surface area in the range of i to 3 〇〇 m 2 /g. Ding electro-acupuncture, for example, in metal-air battery packs, for example, in cadmium-air battery packs, Shao. Pool Group or iron-air battery packs, and especially Zn•air battery packs; 156873.doc 201228081. The invention further relates to a method of making an electrochemical cell of the invention' and a method of making the electrode of the invention. [Prior Art] An alternative to conventional electrochemical cells has been studied for many years. In conventional electrochemical cells, charge transport is carried out to some extent by hydrated protons, and thus the maximum voltage is limited. One of the alternatives to the storage medium for electrical energy is a lithium ion battery pack in which charge transport is ensured by lithium ions in a non-aqueous solvent. However, many of these battery packs are sensitive to air and moisture, which in the worst case can cause spontaneous combustion of the defective lithium ion battery. Furthermore, electrochemical cells are expected to have high energy density. An improvement is provided by a metal-air battery pack (e.g., a word battery). In a common embodiment, the metal (e.g., rhodium) is oxidized by atmospheric oxygen in the presence of an inert electrolyte to form an oxide or hydroxide. The release of the pound is electrochemically utilized. Such a battery pack can be recharged by resuming metal ions formed in the discharge. For this purpose, it is known to use a gas diffusion electrode (GDE) as a cathode. The gas diffusion electrode is porous r and has a dual function. The metal_air battery must be capable of reducing atmospheric oxygen to hydroxide ions during discharge and oxidizing hydroxide ions to oxygen during charging. For this purpose, for example, it is known that the gas diffusion electrode is located on a carrier material composed of finely dispersed carbon, the carrier material comprising a catalyst for catalyzing oxygen reduction or oxygen evolution &amp; or poly(tetra). The choice of catalyst here is very important. In this paper, the following distinctions are described: pure discharge catalysts, for example, metal oxides, for example, on 〇 2, 156873.doc 201228081

Co304、La203、LaNi〇3、NiC〇2〇4、LaMn〇3 及 LaNi〇3 ;金 屬,例如,Ag ;金屬錯合物,例如,CoTMMP(四甲氧基 笨基卟啉)及FeTMMP-Cl ;金屬氮化物,如Mn4N、CrN、 Fe2N ;金屬碳化物,如TaC、TiC及WC ;及雙功能觸媒, 例如,約鈦礦,如 La〇.8Sr〇.2B〇3(參見,V· Neburchilov 等 人 ’ J. Power Scources,2010,195,1271)或 La〇.6Ca〇.4Co〇3 (參見 WO 2003/54989)。 WO 2007/065899揭示用於二次金屬-空氣電池組之雙功 能觸媒,其中電極之活性層包含氧氣還原觸媒及選自 La203、Ag20及尖晶石之雙功能觸媒。 US 5,3 1 8,862揭示由石墨、NiS、FeW〇4及WC之結塊混 合物組成之電極材料,該混合物已經鈷塗覆。 自以上引述之先前技藝知曉之所有材料仍可針對以下性 質中之至少一者進行改良·電催化活性、对化學劑性、耐 電化學腐蝕性 '機械穩定性、對載體材料之良好黏性及與 導電碳黑、黏結劑及(若存在)放電觸媒之低相互作用。 【發明内容】 因此’已發現前文定義之電極。 前文所定義電極(於本發明文中亦稱為本發明電極)包 含: (A) 氣體可擴散通過之固體介質,於本發明文中亦稱為 介質(A)或載體(A), (B) 至少一種導電碳質材料, (C) 至少一種有機聚合物, 156873.doc 201228081 (D)至少一種呈顆粒形式之通式⑴之化合物Co304, La203, LaNi〇3, NiC〇2〇4, LaMn〇3 and LaNi〇3; metals such as Ag; metal complexes such as CoTMMP (tetramethoxyphenyl porphyrin) and FeTMMP-Cl Metal nitrides such as Mn4N, CrN, Fe2N; metal carbides such as TaC, TiC and WC; and bifunctional catalysts, for example, about titanium ore, such as La〇.8Sr〇.2B〇3 (see, V· Neburchilov et al. 'J. Power Scources, 2010, 195, 1271) or La 〇. 6 Ca 〇 . 4 Co 〇 3 (see WO 2003/54989). WO 2007/065899 discloses a dual function catalyst for a secondary metal-air battery, wherein the active layer of the electrode comprises an oxygen reduction catalyst and a dual function catalyst selected from the group consisting of La203, Ag20 and spinel. No. 5,3,8,862 discloses an electrode material consisting of agglomerated mixtures of graphite, NiS, FeW〇4 and WC which have been coated with cobalt. All materials known from the prior art cited above may still be modified for at least one of the following properties: electrocatalytic activity, chemical chemistry, electrochemical corrosion resistance, mechanical stability, good adhesion to carrier materials, and Conductive carbon black, binder and, if present, low interaction of the discharge catalyst. SUMMARY OF THE INVENTION Therefore, the electrodes defined above have been found. An electrode as defined above (also referred to herein as an electrode of the invention) comprises: (A) a solid medium through which a gas can diffuse, also referred to herein as medium (A) or carrier (A), (B) at least A conductive carbonaceous material, (C) at least one organic polymer, 156873.doc 201228081 (D) at least one compound of the formula (1) in the form of particles

MiaM2bMWdHeOf (I) 其中該等變數各定義如下: M1 係選自 Mo、W、V、Nb及 Sb, Μ2 係選自Fe、Ag、Cu、Ni、Μη及鑭系金屬, M3 係選自 Β、C、Ν、Α卜 Si、Ρ及 Sn, M4 係選自 Li、Na、K、Rb、Cs、NH4、Mg、Ca及 Sr, a 係於1至3之範圍内, b 係於0.1至10之範圍内, c 係於0至1之範圍内, d 係於0至1之範圍内, e 係於0至5之範圍内, f 係於1至28之範圍内, 及其中通式(I)之化合物具有在1至300 m2/g範圍内之BET表 面積。 【實施方式】 於本發明文中,氣體可擴散通過之固體介質(亦簡稱為 介質(A))較佳亦視為即使未施加高壓仍可使氧氣或空氣擴 散通過之彼等多孔主體,例如,金屬網狀物及由碳(尤其 活性碳)構成之氣體擴散介質及碳覆金屬網狀物。例如, 可類似於紙或紙板之透氣性的測量,藉由格利(Gurley)方 法測定透氣性。 於本發明之一實施例中。介質(A)具有在20至1000秒/10 156873.doc 201228081MiaM2bMWdHeOf (I) wherein the variables are defined as follows: M1 is selected from the group consisting of Mo, W, V, Nb and Sb, Μ2 is selected from the group consisting of Fe, Ag, Cu, Ni, Μ and lanthanide metals, and M3 is selected from lanthanum, C, Ν, SiSi, Ρ and Sn, M4 is selected from the group consisting of Li, Na, K, Rb, Cs, NH4, Mg, Ca and Sr, a is in the range of 1 to 3, and b is in the range of 0.1 to 10. Within the range, c is in the range of 0 to 1, d is in the range of 0 to 1, e is in the range of 0 to 5, f is in the range of 1 to 28, and its formula (I The compound has a BET surface area in the range of from 1 to 300 m2/g. [Embodiment] In the present invention, a solid medium through which a gas can diffuse (also referred to as medium (A) for short) is preferably also considered to be a porous body through which oxygen or air can diffuse even if no high pressure is applied, for example, a metal mesh and a gas diffusion medium composed of carbon (especially activated carbon) and a carbon-coated metal mesh. For example, the gas permeability can be measured by the Gurley method similar to the measurement of the gas permeability of paper or paperboard. In an embodiment of the invention. Medium (A) has between 20 and 1000 seconds/10 156873.doc 201228081

Cm3空氣’較佳40至120秒/10 cm3範圍内之孔隙度。於本文 中’秒表示「格利秒」。 於本發明之一實施例中 礙地流過介質(A)。 於本發明之一實施例中 ,空氣或大氣氧氣可基本上無阻 ’介質(A)係傳導電流之介質。 於本發明之一較佳實施例中,介質(A)係相對在標準操 作中(即’於充電期間及放電期間)於電化學電池中進行之 反應呈化學惰性。 於本發明之一實施例中’介質係選自具有在2〇至 1500 m2/g範圍内之内bet表面積(較佳稱為表觀bet表面 積)的碳。 於本發明之一實施例中,介質(A)係選自金屬網狀物, 例如鎳網狀物或鈕網狀物。金屬網狀物可粗可細。 於本發明之另一實施例中’介質係選自包含金屬絲 之織物、氈片、毛氈或不織布。 於本發明之一實施例中,介質係選自氣體擴散介質,例 如,活性碳、摻雜鋁之氧化辞、摻雜銻之氧化錫或多孔碳 化物或氮化物’例如’ wc、M〇2c、m〇2n、TiN、ZrN或 TaC。 本發明電極進一步包含至少一種導電碳質材料(B)(於本 發明文中亦稱為導電碳(B))。 導電碳(B)可係選自(例如)石墨、活性碳、碳黑、碳奈米 管、石墨烯或上述物質中至少兩者之混合物。 於本發明之一實施例中,導電碳(B)係碳黑。碳黑可(例 156873.doc 201228081 如)係選自燈黑、爐法碳黑、火焰碳黑、熱碳黑、乙快黑 及工業碳黑。碳黑可包含雜質,例如烴,尤其係芳族和, 或含氧化合物或含氧基團,例如〇H*。此外,碳黑中亦 可能存在含硫或含鐵雜質。 於介質(A)及導電碳(B)各係選擇為活性碳之情況中,基 質(A)與導電碳(B)可於化學上不同或較佳相同。 導電碳(B)可以(例如)具有在(^至丨⑽mm,較佳2至2〇 μιη範圍内之直徑之顆粒形式存在。 於一變型中,導電碳(Β)係經部份氧化之碳黑。 於本發明之一實施例中,導電碳(Β)包含碳奈米管。已 熟知碳奈米管(簡稱為CNT),例如,單壁碳奈米管(sw CNT)及較佳多壁碳奈米管(MW CNT)。其製造方法及一些 性質係(例如)由A_ jess等人描述於Chemie “訌…以The Cm3 air' is preferably a porosity in the range of 40 to 120 seconds/10 cm3. In this article, 'seconds' means "Geli seconds." In one embodiment of the invention, flow through the medium (A) is impeded. In one embodiment of the invention, air or atmospheric oxygen may be substantially unimpeded. Medium (A) is a medium that conducts electrical current. In a preferred embodiment of the invention, the medium (A) is chemically inert with respect to the reaction in an electrochemical cell during standard operation (i.e., during charging and during discharge). In one embodiment of the invention, the medium is selected from carbon having a bet surface area (preferably referred to as an apparent bet surface area) in the range of from 2 Torr to 1500 m2/g. In one embodiment of the invention, the medium (A) is selected from a metal mesh, such as a nickel mesh or a button mesh. The metal mesh can be thick and thin. In another embodiment of the invention, the medium is selected from the group consisting of a fabric comprising a wire, a mat, a felt or a non-woven fabric. In one embodiment of the invention, the medium is selected from the group consisting of a gas diffusion medium, for example, activated carbon, oxidized aluminum-doped, tin-doped tin oxide or porous carbide or nitride 'eg 'wc, M〇2c , m〇2n, TiN, ZrN or TaC. The electrode of the present invention further comprises at least one electrically conductive carbonaceous material (B) (also referred to herein as electrically conductive carbon (B)). The conductive carbon (B) may be selected from, for example, graphite, activated carbon, carbon black, carbon nanotubes, graphene or a mixture of at least two of the foregoing. In one embodiment of the invention, the electrically conductive carbon (B) is carbon black. Carbon black (eg, 156873.doc 201228081) is selected from the group consisting of lamp black, furnace carbon black, flame carbon black, hot carbon black, B fast black, and industrial carbon black. The carbon black may contain impurities such as hydrocarbons, especially aromatic and, or oxygenates or oxygen-containing groups, such as hydrazine H*. In addition, sulfur or iron-containing impurities may also be present in the carbon black. In the case where the medium (A) and the conductive carbon (B) are selected as activated carbon, the matrix (A) and the conductive carbon (B) may be chemically different or preferably identical. The conductive carbon (B) may, for example, be present in the form of particles having a diameter in the range of (^ to 丨(10) mm, preferably 2 to 2 〇μηη. In one variation, the conductive carbon (Β) is a partially oxidized carbon. In one embodiment of the invention, the conductive carbon (cerium) comprises a carbon nanotube. Carbon nanotubes (abbreviated as CNT), such as single-wall carbon nanotubes (sw CNT), are preferred. Wall carbon nanotubes (MW CNT). Its manufacturing method and some properties (for example) are described by A_ jess et al. in Chemie “讧...

Technik 2006,78,94-100 中。 於本發明之一實施例中,碳奈米管具有在0.4至50 nm, 較佳1至25 nm範圍内之直徑。 於本發明之一實施例中,碳奈米管具有在 mm,較佳100 11111至5〇〇 nm.圍内之長度。 可藉由已熟知方法製備碳奈米管。例如,可於一或多種 還原例如’氫氣)及/或另—氣體(例如,氮氣)存在下分 碳化合物(例如’甲烧或一氧化碳、乙炔或乙稀) 氣俨 '人:炭化合物之混合物(例如’合成氣體)。另-適宜 物係一氧化碳與乙稀之混合物。用於分解之適宜 恤又係(例如)於彻至⑽代之範圍内,較佳卿謂代。 156873.doc 201228081 用於分解之適宜壓力條件係(例如)於 知準壓力至100巴 (bar),較佳至1〇巴之範圍内。 可(例如)藉由在光弧中,特定言之在分解觸媒存在或不 存在下分解含碳化合物來獲得單壁或多壁碳奈米管。 於-實施例中,揮發性含碳化合物或含碳化合^之分解 係於分解觸媒(例如,Fe、Co或較佳Ni)存在下進行。 於本發明文中,石墨烯應理勞為意指具有類似於單一石 墨層之結構之幾近理想或理想的二維六角碳晶體。 於本發明之-實施例中,導電碳⑻及尤其碳黑具有依 ISO 9277測量在20至1500 m2/g範圍内之BET表面積。 本發明電極包含至少一種有機聚合物’簡稱為聚合物 (C)或黏結劑(C)。於本文中,術語「有機聚合物」亦包括 有機共聚物,及係指主鏈主要含碳原子(即,至少5〇 mol%),且可藉由自由基聚合、陰離子、陽離子或催化聚 合,或藉由加成聚合或縮合聚合製備之聚合化合物。 特別適宜之聚合物(C)可係選自(例如)可藉由陰離子、催 化或自由基(共)聚合反應獲得之(共)聚合物,尤其係選自 聚乙烯、聚丙烯腈、聚丁二烯、聚苯乙烯、聚乙烯亞胺及 選自乙烯、丙烯、苯乙烯、(甲基)丙烯腈及i,3-丁二烯之 至少兩種共單體之共聚物。聚丙稀亦適宜。聚異戊二稀及 聚丙烯酸酯亦適宜。特佳者係聚丙烯腈。 於本發明文中’聚丙烯腈應理解為不僅意指聚丙烯腈均 聚物’而且意指丙烯腈與1,3_丁二稀或苯乙烯之共聚物。 較佳者係聚丙烯腈均聚物。 156873.doc 10· 201228081 於本發明文中,聚乙烯不僅應理解為意指均聚乙烯,而 且亦意指包含至少50 mol%共聚乙烯及至多5〇 mol%之至少 一種其他共單體(例如,α_烯烴,如丙烯、丁烯(丨丁烯)、 1-己烯、1-辛烯、1_癸烯、1_十二烯、卜戊烯及異丁烯; 乙烯基芳烴,例如,苯乙烯;及(曱基)丙烯酸、乙酸乙烯 酯、丙酸乙烯酯、(甲基)丙烯酸之Ci_Ci〇烷基酯,尤其丙 烯酸甲酯、甲基丙烯酸曱酯、丙烯酸乙酯、曱基丙烯酸乙 酯、丙烯酸正丁酯、丙烯酸2_乙基己酯、甲基丙烯酸正丁 酯、曱基丙烯酸2-乙基己酯;及馬來酸、馬來酸酐及衣康 酸野)之乙烯共聚物。聚乙烯可為HDPE或LDPE。 於本發明文中’聚丙烯不僅應理解為意指均聚丙烯,而 且意指包含至少50 m〇l%共聚丙烯及至多5〇 m〇1%之至少另 一共單體(例如,乙烯及α_烯烴,如丁烯、卜己烯、丨_辛 稀1癸稀、1_十二烯及1_戊稀)之丙烯共聚物。聚丙烯較 佳係等規或基本上等規聚丙烯。 於本發明文中,聚苯乙稀不僅應理解為意指苯乙烯之均 聚物,而且意指與丙烯腈、丨,3_丁二烯、(甲基)丙烯酸、 (曱基)丙烯酸烷基酯、二乙烯基苯,尤其i,3-二乙 烯基苯、1,2-二苯基乙烯及〇_甲基苯乙烯之共聚物。 另一較佳黏結劑(聚合物(c))係聚丁二烯。 其他適且聚合物(c)係選自聚環氧乙烷(pE〇)、纖維素、 羧曱基纖維素、聚醯亞胺及聚乙烯醇。 於本發明之一實施例中,聚合物(c)係選自具有在5〇 〇⑼ 至1 000 〇〇〇 g/m〇i,較佳至5〇〇 〇〇〇 g/m〇l範圍内之平均分 156873.doc •11· 201228081 子量%货之彼等(共)聚合物。 聚合物(c)可為交聯或未交聯(共)聚合物。 於本發明之一特佳實施例中,聚合物⑹係選自鹵化(共) 聚合物’尤其選自I化(共)聚合物4化或氟化(共)聚: 物應理解為意指包含至少一種每分子具有至少一㈣^ 或至少-個敦原子,較佳每分子至少兩個齒原子或至少兩 個氟原子之(共)聚合(共)單體之彼等(共)聚合物。 實例係聚氯乙烯、聚偏二氣乙烯、聚四氟乙烯、聚偏二 氟乙稀、四氟乙烯-六氣丙埽共聚物、偏二氟乙烯_六氟丙 稀共聚物(PVdF-HFP)、偏二氟乙烯_四氟乙烯共聚物全 敦烧基乙稀基驗共聚物、乙稀_四氟乙烯共聚物、偏二氟 乙烯-氣二氟乙烯共聚物及乙烯_氣氟乙烯共聚物。 適且聚合物(C)尤其係聚乙烯醇及鹵化(共)聚合物,例如 聚氣乙稀或聚偏二氯乙烯,尤其氟化(共)聚合物,如聚敦 乙烯及尤其聚偏二氟乙烯及聚四氟乙稀。 本發明㈣進一纟包含至少一種呈顆㈣式之通式⑴之 化合物 M1aM2bM3cM4dHeOf (|) 亦簡稱為化合物(D) ’其中該等變數各定義如下: ^係選自Mo、W、V、Nb及sb,較佳者係v、M〇及w, Μ2係選自Fe、Ag、Cu、Ni、Μη及鑭系金屬,較佳者係 Fe、Ag及尤其鑭系金屬La及Ce, Μ3 係選自 Μ4 係選自 Li、Na、K、Rb、Cs、NH4、Mg、Cawr^ 156873.doc 12 201228081 佳者係NH4、Li、K及Na, a 係於1至3之範圍内,較佳係1, b 係於0.1至1〇之範圍内,較佳0.3至3, c 係於〇至1 ’較佳至0.2之範圍内, d 係於〇至1,較佳至0.2之範圍内, e 係於〇至5 ’較佳至i.o之範圍内, f 係於1至28之範圍内, 及其中通式(I)之化合物具有在1至3〇〇 m2/g,較佳1至1〇〇 m2/g,更佳1至5〇 m2/g範圍内之BET表面積。 於本發明之一實施例中,變數f係經選擇以使化合物(D) 不帶電荷。 於本發明之另一實施例中,變數f係經選擇以使化合物 (D)非不帶電荷,例如,帶小於〇至_2電荷。 當變數4經選擇為不等於〇時,氫較佳係以氣氧根離子 存在於化合物(D) _。 於本發明之-實施例中,化合物(D)中之m1、m2、m^ μ4係選自至少兩種元素之混合物。例如,係選自Fe 與Ag之混合物。例如,M丨可係選自v_〇之混合物。 於本發明之—實施例中,化合物(d)係選自混合氧化物 及異多元酸及其鹽,例m驗金屬鹽。化合物⑼較 佳係選自混合氧化物。 於本發明之一實施例中,化合物⑼係選IFe_Ag_x_〇、Technik 2006, 78, 94-100. In an embodiment of the invention, the carbon nanotubes have a diameter in the range of 0.4 to 50 nm, preferably 1 to 25 nm. In one embodiment of the invention, the carbon nanotubes have a length in the range of mm, preferably 100 11111 to 5 〇〇 nm. The carbon nanotubes can be prepared by well-known methods. For example, a carbon-containing compound (eg, 'methyl or carbon monoxide, acetylene, or ethylene) may be present in the presence of one or more reductions such as 'hydrogen' and/or another gas (eg, nitrogen). (eg 'synthetic gas'). Alternatively - a suitable mixture of carbon monoxide and ethylene. The suitability for decomposition is, for example, within the scope of (10) generations. 156873.doc 201228081 Suitable pressure conditions for decomposition are, for example, within a range of 100 bar, preferably 1 bar. Single or multi-walled carbon nanotubes can be obtained, for example, by decomposing carbonaceous compounds in the arc of light, specifically in the presence or absence of a decomposition catalyst. In the embodiment, the decomposition of the volatile carbon-containing compound or the carbon-containing compound is carried out in the presence of a decomposition catalyst (e.g., Fe, Co or preferably Ni). In the context of the present invention, graphene is meant to mean a nearly ideal or ideal two-dimensional hexagonal carbon crystal having a structure similar to a single graphite layer. In the embodiment of the invention, the electrically conductive carbon (8) and in particular the carbon black have a BET surface area in the range from 20 to 1500 m2/g as measured by ISO 9277. The electrode of the present invention comprises at least one organic polymer 'abbreviated as polymer (C) or binder (C). As used herein, the term "organic polymer" also includes organic copolymers, and means that the main chain contains predominantly carbon atoms (ie, at least 5 mole %) and can be polymerized by free radical polymerization, anionic, cationic or catalytic polymerization. Or a polymeric compound prepared by addition polymerization or condensation polymerization. Particularly suitable polymers (C) may be selected, for example, from (co)polymers obtainable by anionic, catalytic or free radical (co)polymerization, especially selected from the group consisting of polyethylene, polyacrylonitrile, polybutylene a copolymer of a diene, a polystyrene, a polyethyleneimine, and at least two comonomers selected from the group consisting of ethylene, propylene, styrene, (meth)acrylonitrile, and i,3-butadiene. Polypropylene is also suitable. Polyisoprene and polyacrylates are also suitable. The most preferred one is polyacrylonitrile. As used herein, &quot;polyacrylonitrile&quot; is understood to mean not only a polyacrylonitrile homopolymer&apos; but also a copolymer of acrylonitrile and 1,3-butadiene or styrene. Preferred are polyacrylonitrile homopolymers. 156873.doc 10· 201228081 In the context of the present invention, polyethylene is understood not only to mean homopolyethylene, but also to mean at least 50 mol% of copolyethylene and up to 5 mol% of at least one other co-monomer (for example, _-olefins such as propylene, butene (butene), 1-hexene, 1-octene, 1-decene, 1-dodecene, pentene and isobutylene; vinyl aromatic hydrocarbons, for example, styrene And (indenyl) acrylic acid, vinyl acetate, vinyl propionate, Ci_Ci decyl (meth) acrylate, especially methyl acrylate, methacrylate, ethyl acrylate, ethyl methacrylate, An ethylene copolymer of n-butyl acrylate, 2-ethylhexyl acrylate, n-butyl methacrylate, 2-ethylhexyl methacrylate; and maleic acid, maleic anhydride, and itaconic acid. The polyethylene can be HDPE or LDPE. In the context of the present invention, 'polypropylene is understood to mean not only homopolypropylene, but also means at least 50 m〇l% of copolypropylene and at most 5〇m〇1% of at least one other co-monomer (for example, ethylene and α_). A propylene copolymer of an olefin such as butene, hexylene, hydrazine, hydrazine, 1 undoxene and pentylene. Polypropylene is preferably isotactic or substantially isotactic polypropylene. In the context of the present invention, polystyrene is understood to mean not only a homopolymer of styrene but also an alkyl group with acrylonitrile, hydrazine, 3-butadiene, (meth)acrylic acid, (meth)acrylic acid. Copolymer, divinylbenzene, especially copolymer of i,3-divinylbenzene, 1,2-diphenylethylene and fluorene-methylstyrene. Another preferred binder (polymer (c)) is polybutadiene. Further suitable polymers (c) are selected from the group consisting of polyethylene oxide (pE), cellulose, carboxymethyl cellulose, polyimine and polyvinyl alcohol. In one embodiment of the invention, the polymer (c) is selected from the group consisting of having a range of from 5〇〇(9) to 1 000 〇〇〇g/m〇i, preferably up to 5〇〇〇〇〇g/m〇l The average score within the 156873.doc •11·201228081 sub-quantity of the goods of the (co)polymer. The polymer (c) may be a crosslinked or uncrosslinked (co)polymer. In a particularly preferred embodiment of the invention, the polymer (6) is selected from a halogenated (co)polymer, which is selected, inter alia, from a (co)polymer or a fluorinated (co)polymer: a (co)polymer comprising at least one (co)polymerized (co)monomer having at least one (four) or at least one atomic atom per molecule, preferably at least two tooth atoms per molecule or at least two fluorine atoms . Examples are polyvinyl chloride, polyvinylidene oxide, polytetrafluoroethylene, polyvinylidene fluoride, tetrafluoroethylene-hexafluoropropene copolymer, vinylidene fluoride-hexafluoropropylene copolymer (PVdF-HFP) ), a vinylidene fluoride-tetrafluoroethylene copolymer, a terpene-based ethylene-based copolymer, an ethylene-tetrafluoroethylene copolymer, a vinylidene fluoride-gas difluoroethylene copolymer, and an ethylene-gas fluoroethylene copolymer. Things. Suitable polymers (C) are, in particular, polyvinyl alcohols and halogenated (co)polymers, such as polyethylene or polyvinylidene chloride, especially fluorinated (co)polymers, such as polydivinyl and especially polypyridyl Vinyl fluoride and polytetrafluoroethylene. The present invention (4) further comprises at least one compound M1aM2bM3cM4dHeOf (|) of the formula (1) of the formula (4), which is also simply referred to as the compound (D) ' wherein the variables are defined as follows: ^ is selected from the group consisting of Mo, W, V, Nb and Sb, preferably v, M〇 and w, Μ2 is selected from the group consisting of Fe, Ag, Cu, Ni, Μ and lanthanide metals, preferably Fe, Ag and especially lanthanide metals La and Ce, Μ3 Self-Μ 4 is selected from the group consisting of Li, Na, K, Rb, Cs, NH4, Mg, and Cawr^ 156873.doc 12 201228081 The best is NH4, Li, K and Na, a is in the range of 1 to 3, preferably 1, b is in the range of 0.1 to 1 ,, preferably 0.3 to 3, c is in the range of 〇 to 1 'preferably to 0.2, and d is in the range of 〇 to 1, preferably to 0.2, e It is in the range of 5' to io, f is in the range of 1 to 28, and the compound of the formula (I) thereof has 1 to 3 〇〇m2/g, preferably 1 to 1 〇. 〇m2/g, more preferably BET surface area in the range of 1 to 5 〇 m 2 /g. In one embodiment of the invention, the variable f is selected such that the compound (D) is uncharged. In another embodiment of the invention, the variable f is selected such that the compound (D) is non-charged, e.g., the band is less than 〇 to _2. When the variable 4 is selected to be not equal to 〇, hydrogen is preferably present in the compound (D) _ with the oxy-ion ion. In the embodiment of the present invention, m1, m2, and m^4 in the compound (D) are selected from a mixture of at least two elements. For example, it is selected from a mixture of Fe and Ag. For example, M丨 can be selected from a mixture of v_〇. In the examples of the present invention, the compound (d) is selected from the group consisting of mixed oxides and isopolyacids and salts thereof. The compound (9) is preferably selected from the group consisting of mixed oxides. In an embodiment of the invention, the compound (9) is selected from IFe_Ag_x_〇,

Fe-v-X-〇、Ag x 〇,其中X係選自鶴 及較佳鉬。 156873.doc •13· 201228081 於本發明之一實施例中 自通式(II)之化合物 化合物⑴中之Fe-Ag-Χ-Ο係選Fe-v-X-〇, Ag x 〇, wherein X is selected from the group consisting of cranes and preferably molybdenum. 156873.doc •13·201228081 In an embodiment of the invention, the Fe-Ag-Χ-Ο system in the compound (1) from the compound of the formula (II)

XeFebiAgb2〇f 00 其中變數bl與b2之和係於〇.丨至1〇 及其餘變數各係如上所定義。 於本發明之一實施例中,Fe_v_x_〇係選自 合物 較佳0.3至3之範圍内, 通式(III)之化XeFebiAgb2〇f 00 wherein the sum of the variables bl and b2 is 〇.丨 to 1〇 and its covariates are as defined above. In one embodiment of the present invention, Fe_v_x_〇 is selected from the group consisting of preferably 0.3 to 3, and the formula (III)

ValXaiFebOf (III) 其中變數al與a2之和係於 餘變數各係如上定義。 於本發明之一實施例令 合物 1至3之範圍内及較佳係1,及其 ’ Ag-V-Χ-Ο係選自通式(IV)之化ValXaiFebOf (III) wherein the sum of the variables al and a2 is defined by the remainder of the remainder. In the range of the compositions 1 to 3 and preferred in the embodiment of the present invention, and the 'Ag-V-Χ-Ο system is selected from the group consisting of the formula (IV)

VaiXa2Agb〇f 其中該等變數各係如上定義 於本發明之一實施例中 合物 (IV)VaiXa2Agb〇f wherein the variables are as defined above in an embodiment of the invention (IV)

Ce-x-0係選自通式(V)之化 ^ (V) 其中該等變數各係如上定義。 化合物(D)係呈顆粒形式。 « Ml, '於此情況中,該等顆粒可為 規則或不規則形狀且具有 規則形狀。 ]如)球形、小板形、針形或不 於本發明之—實施例 IS e 、 化σ物⑴)具有在10至50 nmg 固内之+均初級粒徑。 礼 如,_由# X π 句初級粒徑可藉由顯微鏡,例 精甶和描式電子顯 *' 兄或藉由穿透式電子顯微鏡 156873.doc •14· 201228081 (TEM)測定。 於本發明之—實施例中,化合物⑼係呈聚結顆粒之形 :二此情況中,該等聚結物可具有2。赠1〇〇叫之平 :。於此情況中,聚結物可具有使化合物⑼之顆粒 〇列如)至少兩至數千個初級顆粒構成之外觀。 旦於本發明之一實施例中’化合物(D)具有依IS0 9277測 里在1至30〇m2/^_之Μτ表面積。 於本發明之_實施例中,化合物⑼具有雙峰式粒徑分 佈。 於本發明之—實施例中,本發明電極包含至少兩不同化 合物(D)之混合物。 於本發明之—實施例中,本發明電極包含基於總電極: 在20至50重量%,較佳35至45重量%範圍内之導電碳⑻, 在5至45重量%,較佳3〇至4〇重量%範圍内之聚合_, 及 在〇.5至25重量%’較佳5至15重量%範圍内之化合物(1))。 於本發明之一實施例中,本發明電極進一步包含至少一 種放電觸媒(E)。 適宜放電觸媒(E)之實例為(例如)La2〇3、Ag2〇、尖晶 石,例如,LiMn204、Mn02、Ag、CoTMMP(四[對甲氧基 本基]卟琳姑)、FeTMMP-Cl、Mn4N、CrN、Fe2N、TaC、 TiC、WC、Co304、La203、LaNi〇3、NiCo204、LaMn03、Ce-x-0 is selected from the group consisting of the formula (V) ^ (V) wherein the variables are as defined above. Compound (D) is in the form of particles. « Ml, 'In this case, the particles may be regular or irregular in shape and have a regular shape. For example, a spherical shape, a small plate shape, a needle shape or not according to the present invention - the embodiment IS e , the yttrium compound (1)) has a + average primary particle diameter within 10 to 50 nmg of solid. Etiquette, _ by # X π sentence primary particle size can be determined by microscope, for example, fine and tracing electrons *' brother or by transmission electron microscope 156873.doc •14·201228081 (TEM). In the embodiment of the present invention, the compound (9) is in the form of coalesced particles: in this case, the agglomerates may have 2. Give 1 〇〇 之 平 :. In this case, the agglomerates may have an appearance in which the particles of the compound (9) are, for example, at least two to several thousands of primary particles. In one embodiment of the present invention, the compound (D) has a 表面积τ surface area of from 1 to 30 〇 m 2 / _ in accordance with IS0 9277. In the embodiment of the present invention, the compound (9) has a bimodal particle size distribution. In an embodiment of the invention, the electrode of the invention comprises a mixture of at least two different compounds (D). In an embodiment of the invention, the electrode of the invention comprises based on the total electrode: conductive carbon (8) in the range of 20 to 50% by weight, preferably 35 to 45% by weight, in 5 to 45% by weight, preferably 3 to Polymerization _ in the range of 4% by weight, and compound (1) in the range of 55 to 25% by weight, preferably 5 to 15% by weight. In one embodiment of the invention, the electrode of the invention further comprises at least one discharge catalyst (E). Examples of suitable discharge catalysts (E) are, for example, La2〇3, Ag2〇, spinel, for example, LiMn204, Mn02, Ag, CoTMMP (tetrakis-p-methoxybenzamine), FeTMMP-Cl , Mn4N, CrN, Fe2N, TaC, TiC, WC, Co304, La203, LaNi〇3, NiCo204, LaMn03,

LaNi〇3,尤其 Ag 及 Ag/C。 放電觸媒(E)較佳係呈顆粒形式。於此情況中,顆粒可 156873.doc 15· 201228081 為規則或不規則形狀,及具有(例如)球形、小板形、針形 或不規則形狀。放電觸媒顆粒之平均直徑可係於2 nm至 100 μιη之範圍内。Ag之顆粒(於本發明文中亦稱為Ag顆粒) 可(例如)具有在2至200 nm,較佳1 0至50 nm範圍内之平均 直徑。若希望使用Ag覆碳作為放電觸媒,則Ag顆粒可具 有於2至200 nm範圍内之直徑,及碳顆粒具有於〇1至1〇〇 μπι範圍内之直徑。 於本發明電極包含至少一放電觸媒(Ε)之實施例中,本 發明電極包含基於導電碳(Β)、聚合物((:)及化合物(D)之總 和a十在〇· 5至80重量。/〇範圍内之放電觸媒(E)。 於本發明電極包含Ag顆粒作為放電觸媒(E)之較佳實施 例中,本發明電極包含基於導電碳(B)、聚合物及化合 物(D)之總和計在〇.5至15重量%,較佳2至6重量%範圍内之 放電觸媒(E)。 於本發明電極包含Ag顆粒覆碳作為放電觸媒(E)之較佳 實施例中,本發明電極包含基於導電碳⑻、聚合物⑹及 &amp;物(D)之總和计在1 〇至8〇重量% ’較佳至%重量%範 圍内之放電觸媒(E)。 於本發明之-實施例中,本發明電極可具有其他組分。 適宜的其他組分係(例如)溶劑’其應理解為意指有機溶 劑:尤其異丙醇、N_甲基。比。各相、n,n_:甲基乙醯胺、 、’正丙醇或私己酮。更適宜的溶劑係環狀或非環狀有 機碳酸醋’例如,碳酸二乙0旨、碳酸伸乙g|、碳酸伸丙 醋、碳酸二甲醋及碳酸乙@旨甲3旨;及環狀或非環狀有機 156873.doc 201228081 及環狀或非 醋’例如’甲酸甲醋、乙酸乙醋或γ_丁内醋 環狀醚,例如,丨,3_二氧雜環戊烷。 此外’本發明電極可包含水。 二:明電極可以各種形式構造。例如,於載體⑷係選 自金屬網狀物之情況中,本發明電極之形式基本上可由金 屬柵格之形式定義。 此外’於載體⑷係選自活性碳之情況中在精細分散 之活性碳(例如’具有在H1〇〇帥範圍内之平均粒徑)之 情況下,電極係以調配物(例如,以糊料或膠糊)施用至金 屬網狀物、由碳構成之氣體擴散介質或由碳覆金屬網狀物 構成之氣體擴散介質。 本發明進-步提供本發明電極於電化學電池,例如,於 不可再充電之電化學電池(亦稱為原電池組)或於可再充電 :化學電池(亦稱為二次電池組)中之用途。本發明進一步 提供-種利用至少-個本發明電極製造電化學電池之方 法本發明進一步提供包含至少一個本發明電極之電化學 電池。 於本發明之一較佳實施例中,本發明電化學電池包含LaNi〇3, especially Ag and Ag/C. The discharge catalyst (E) is preferably in the form of particles. In this case, the particles may be regular or irregular in shape, and have, for example, a spherical shape, a small plate shape, a needle shape or an irregular shape. The average diameter of the discharge catalyst particles can be in the range of 2 nm to 100 μm. The particles of Ag (also referred to herein as Ag particles) may, for example, have an average diameter in the range of 2 to 200 nm, preferably 10 to 50 nm. If it is desired to use Ag-coated carbon as a discharge catalyst, the Ag particles may have a diameter in the range of 2 to 200 nm, and the carbon particles have a diameter in the range of 〇1 to 1 〇〇 μπι. In an embodiment in which the electrode of the present invention comprises at least one discharge catalyst (Ε), the electrode of the present invention comprises a total of a conductive carbon (Β), a polymer ((:), and a compound (D) a ten in the range of 5 to 80 Discharge catalyst (E) in the range of weight / 〇. In a preferred embodiment in which the electrode of the present invention comprises Ag particles as a discharge catalyst (E), the electrode of the present invention comprises conductive carbon (B), a polymer and a compound. The sum of (D) is in the range of 55 to 15% by weight, preferably 2 to 6% by weight, of the discharge catalyst (E). The electrode of the present invention comprises Ag particles covered with carbon as a discharge catalyst (E). In a preferred embodiment, the electrode of the present invention comprises a discharge catalyst (E) in the range of from 1 Torr to 8% by weight of 'conductive to % by weight based on the total of conductive carbon (8), polymer (6) and &amp; (D). In the present invention, the electrode of the present invention may have other components. Suitable other components are, for example, a solvent, which is understood to mean an organic solvent: especially isopropanol, N-methyl. Specific phase, n, n_: methyl acetamide, 'n-propanol or hexanone. More suitable solvent ring Or acyclic organic carbonated vinegar 'for example, carbonic acid diethylation, carbonic acid extension g |, carbonic acid propylene vinegar, carbonic acid dimethyl vinegar and ethylene carbonate @ 甲甲3; and cyclic or acyclic organic 156873. Doc 201228081 and cyclic or non-vinegar 'for example 'methyl formate, ethyl acetate or γ-butane vine cyclic ether, for example, hydrazine, 3 -dioxolane. Furthermore, the electrode of the invention may comprise water. Second, the bright electrode can be constructed in various forms. For example, in the case where the carrier (4) is selected from a metal mesh, the form of the electrode of the present invention can be substantially defined by the form of a metal grid. Further, the carrier (4) is selected from activated carbon. In the case of finely dispersed activated carbon (eg, having an average particle size within the range of H1), the electrode is applied to the metal mesh as a formulation (eg, as a paste or paste). a gas diffusion medium composed of carbon or a gas diffusion medium composed of a carbon-coated metal mesh. The present invention further provides an electrode of the invention to an electrochemical cell, for example, a non-rechargeable electrochemical cell (also referred to as Primary battery pack) or rechargeable Use in a chemical battery (also referred to as a secondary battery pack). The invention further provides a method of making an electrochemical cell using at least one electrode of the invention. The invention further provides an electrochemical cell comprising at least one electrode of the invention. In a preferred embodiment of the invention, the electrochemical cell of the invention comprises

Cd-空氣電池組、Fe_空氣電池組、A1空氣電池組或鋅·空 氣電池組。 本發明電化學電池可具有其他成份,例如,可呈任意形 狀,尤其圓柱形、圓盤形或長方體形之外殼,及至少一相 反電極。該相反電極包含作為必需成份之呈元素形式之金 屬’例如,Fe、A卜Cd或尤其鋅》 156873.doc •17- 201228081 呈元素形式之金屬可呈固體厚片、燒結多孔電極或金屬 粉末或球粒之形式,其視需要經燒結。於一實施例中,金 属(尤其鋅)係呈作為具有(例如)2 μιη至500 μιη,較佳30 至100 μιη範圍内之平均粒徑(數量平均值)之粉末之元素形 式。 於一實施例中,將呈粉末形式之金屬與有機黏結劑混合 以改良尺寸穩定性。適宜的有機黏結劑係聚砜、聚醚砜及 尤其氟化(共)聚合物,例如,聚四氟乙烯(pTFE)及聚偏二 氟乙烯(PVDF)。 於一較佳實施例中,將呈粉末形式之金屬,尤其呈粉末 形式之鋅’以與有機黏結劑之糊料或膠糊使用。 本發明電化學電池可進一步包含將帶不同電荷之電極彼 此機械分離之至少一間隔物,藉此防止短路。適宜的間隔 物係聚合物膜’尤其係多孔聚合物膜,其等對呈元素狀態 之金屬及於本發明電化學電池中一般呈強鹼性之介質不具 反應性。用於間隔物之特別適宜的材料係聚烯烴,尤其多 孔聚乙烯膜及多孔聚丙烯膜。 聚稀烴間隔物,尤其聚乙烯或聚丙烯間隔物,可具有在 35至45。/〇範圍内之孔隙度。適宜的孔徑係(例如)於3〇至5〇〇 nm之範圍内。 於本發明之另一實施例中,間隔物可係選自以鹼穩定無 機顆粒填充之PET不織布。此等間隔物可具有在4〇至55〇/〇 範圍内之孔隙度。適宜的孔徑係(例如)於8〇至75〇 nm之範 圍内。 156873.doc 18· 201228081 爲製造本發明電化學電池,程序可為(例如)將本發明電 極、間隔物及相反電極彼此組合及將其等引入具有任何其 他組分之外殼中。 本發明電化學電池可進一步包含至少一種電解質,該電 解質係至少一溶劑與至少一類鹽化合物或鹽之組合。適宜 電解質之實例尤其係水性鹼溶液,例如,氫氧化鈉溶液或 氫氧化卸溶液。 於本發明之一實施例中,本發明電化學電池可包含另一 電極,例如,作為參考電極。適宜的另一電極係(例如)鋅 線。 本發明進一步提供一種製造本發明電極之方法,於下文 中亦稱為本發明製造方法。爲實施本發明製造方法,程序 可為將 (B) 至少一種導電碳質材料, (C) 至少一種有機聚合物,及 (D) 至少一種呈顆粒形式且具有在1至3〇〇 m2/g範圍内 之BET表面積之通式(I)之化合物 以一或多個步驟施用至 (A) 氣體可擴散通過之固體介質。 該程序具體言之可為將 (B) 至少一種導電碳質材料 (C) 至少一種有機聚合物及 (D) 至少一種呈顆粒形式且具有在1至3〇〇 m2/g範圍内 之BET表面積之通式(I)之化合物 156873.doc •19· 201228081 以水性或溶劑性油墨或較佳水性糊料或較佳水性膠糊之 形式施用至 (A)氣體可擴散通過之固體介質。 式(I)之化合物係如上所述。其餘變數亦係如上所述。 亦可先以導電碳(B)處理化合物(D)(例如,塗覆),及隨 後與聚合物(C)混合並施用至載體(a)。 例如,可藉由喷塗(例如,喷塗上或嘴霧)及刮刀塗覆、 印刷或藉由壓製實施塗覆。於本發明文中,喷霧亦包括藉 助喷搶來施用’此方法經常亦稱為「氣刷法」或簡稱: 「氣刷」。 本發明製造方法係(例如)自一或多種化合物(d) 施。 例如,可藉由將視需要⑷及/或m4之適宜化合 物以(例如)乾燥形式或作為溶液或懸浮液彼此混合來製: 化合物(D)。較佳依化合物(D)中之Μ1、Μ,、任何Μ及Μ# 之化學計量來選擇Μ丨、心視需要―以之化合物' 比。以此方式獲得之混合物隨後經熱處$里;例如,盆可 (例如)於250至,較佳遍至刚t範圍内之溫度殘 燒:該锻燒可於惰性氣體或於氧化氛圍,例如空氣(或惰 性氣體與氧氣之另-混合物)下進行。锻燒時間可為數分 鐘至數小時。 可用於製傷化合物⑼之適宜起始物質包括μ1、Μ、W 及MW之氧化物、氣氧化物或經基氧化物。可使用之 M、M2、M3及/或M4之其他此等化合物係於氧氣存在或不 156873.doc 201228081 存在下由於加熱反應而產生氧化物、氫氧化物或經基氧化 物之彼等物。 可將起始物質以乾或濕形式混合而製備化合物(D)。若 需以乾燥形式進行,則可將用於製備化合物(D)之起始物 質以細粉末形式使用,及於混合及視需要壓實後,進行锻 燒。然而’較佳係以濕形式進行密切混合。一般而言,此 涉及將用於製備化合物(D)之起始物f以水溶液及/或懸浮 液之形式彼此混合。 可藉由兀王自呈溶解形式之M丨、M2、M3及/或Μ#之化合 物開始並使Μ、Μ、M3及/或μ4之化合物沉澱而獲得用 於製備化合物(D)之起始物質之特佳混合物。隨後將可藉 此獲得之水性物質在較佳1⑽至15(rc範圍内之溫度下乾 燥極佳之乾燥方法係嘴霧乾燥,尤其係在⑽至^贼 範圍内之出口溫度下之噴霧乾燥。 於熱處理之前、期間或較佳之後,可進行建立所需化合 物⑼粒度之步驟,例如,篩選、研磨或分級。 於視需要步驟中,彳以導電碳⑻處理⑼如,塗覆)化 口物()爲實施此處理,例如,可將化合物(D)與導電碳 (B)充分展合,例如, j如將其研磨。例如,研磨機,尤其球 磨機’適宜用於研磨。 於視需要藉由導電碳⑻處理化合物(D)之另一變型中, 可(例如)藉由分解有機化合物將碳沈積於化合物(D)上。 接著與聚合物(C)混合,該聚合物(C)可(例如)以水性分 散液或球粒之形式添加。 156873.doc -21- 201228081 於另一實施例中,可(例如)藉由將相應固體視需要與一 或多種有機溶劑或與水一起攪拌而以一步驟混合化合物 (D)、導電碳(B)及聚合物(C),其中聚合物(c)可以(例如)水 性分散液或球粒之形式添加。關於混合,例如,可使用諸 如攪拌罐、或研磨機(例如,球磨機及尤其攪拌式球磨機) 之攪拌裝置。於其他實施例中,使用超音波,(例如)藉助 於音極。此獲得較佳水性調配物。 隨後,確定待施用之較佳水性調配物之所需性質,例 如,黏度或固體含量。 於本發明文中,將具有0.5至25%範圍内之固體含量之彼 等較佳水性調配物稱為油墨。將具有大於25%之固體含量 之彼等較佳水性調配物稱為糊料。 於本發明之一實施例中,該較佳水性調配物包含至少一 種表面活性劑。於本發明文中,表面活性劑係表面活性物 質。表面活性劑可係選自陽離子、陰離子及較佳非離子性 表面活性劑。 隨後長1供;|質(A)或載體(A),並將較佳水性調配物或 包含導電碳(B)、聚合物(c)、化合物(D)及任何放電觸媒 (E)之較佳水性調配物以一或多個步驟施用至該介質(a)或 載體⑷。可藉由(例如)施塵、喷塗(尤其藉由喷搶)及到刀 塗覆或較佳印刷來進行該施用。 於本發明之另一實施例中,可(例如)在3〇至3〇〇巴範圍 内之壓力及150至320C範圍内之溫度下,將無溶劑導電碳 (B)聚σ物(C)、化合物(D)及視需要放電觸媒(E)組分之 156873.doc -22- 201228081 混合物彼此壓縮。就此目的而言,可自糊料,較佳自水性 糊料開始,其層高可藉助塾片’藉由滚壓及切割調整至所 需尺寸,及將其施用至所關注之介質(A)。 施用後,可接著(例如)藉由熱處理,尤其在15〇至35〇。(: 範圍内之溫度下,尤其在接近聚合物(c)之玻璃轉化溫度 之溫度下處理來固定。於此情況中,例如,當選擇偏二氟 乙烯-六氟丙烯共聚物作為聚合物(c)時,較佳(例如)於125 至175 C之範圍内選擇該溫度,較佳約i5〇。〇。於另一變型 中,所選擇之溫度為175至225^,較佳約2〇(rc,及所選 擇之聚合物(C)係聚偏二氟乙烯。於另一變型中,所選擇 之溫度為300至350C ’較佳320至325 °C,及所選擇之聚合 物(C)係聚四氟乙烯。 於一變型中,可以機械方式,例如藉由壓延固定。 此獲付本發明電極’其可與其他成份組合以形成本發明 電化學電池。 此獲得具有極佳總體性質之本發明電化學電池。 本發明之另一態樣係調配物,亦簡稱為本發明調配物, 其包含至少一種有機溶劑或水及 (B) 至少一種導電碳質材料; (C) 至少一種有機聚合物及 (D) 至少一種包含鉬或鎢及選自Fe、Ag、鑭系金屬及V 之至少一元素之混合氧化物。 水性調配物為較佳。 導電碳(Β)、聚合物(C)及化合物(D)已於上文定義。 156873.doc • 23- 201228081 於本發明之-實施例中’本發明之較佳水性調配物包含 選自表面活性劑、增稠劑及消泡劑之至少一其他成份。 於本發明之—實施例中,本發明之較佳水性調配物可具 有0.5至60%範圍内之固體含量。 本發明藉由工作實例說明。 基本備註:於本發明文中,除非另外明確說明,否則以 百分比表示之數字係指重量百分比。 I.製造水性調配物 1.1製造水性油墨,WF1.1 於一攪拌容器中,使用磁力攪拌器混合2 g乙氧基化三 甲基壬基醇及66.5 g水。隨後添加〇·4 g Nis、〇 4 g w〇^i g FeAgM〇2〇8(D.1)(BET表面積 1 5 m2/g)及 3 g Ag活性碳 (9%Ag覆〇(Β·υ,同時攪拌。隨後利用超音波藉由以下程 序分散:14 mm US音極,循環卜欠,振幅45% ’ 8。〇冷卻, 磁力攪拌器75〇/。’至大0.025 kWh之能量輸入。隨後添加 3.8 g具有60%固體含量之聚四氟乙烯水性分散液(c i),及 :在無進一步超音波下將混合物攪拌15分鐘。通過一19〇 pm 網篩過濾混合物而獲得本發明油墨,其於下文亦稱為 WF1.1。 1.2製造水性油墨,WF 1.2 於一攪拌容器中,使用一磁力攪拌器來混合2 g乙氧基 化二甲基壬基醇及66.5 g水。隨後添加〇 4 g Nis、〇 4 g WC 及 0.4 g Fe2(W04)3(D.2)(BET 表面積 3 m2/g)及 3 g ^活 性石厌(9〇/〇 Ag覆C)(B. 1),同時授拌。隨後利用超音波藉由以 156873.doc -24· 201228081 下程序分散:14 mm US音極,循環1次,振幅45% ’ 8°C冷 卻’磁力攪拌器75%,至大0.025 kWh之能量輸入。隨後添 加3.8 g具有60%固體含量之聚四氟乙烯水性分散液(C1), 及在無進一步超音波下將混合物攪拌15分鐘。通過一 19〇 μηι網篩過濾混合物而獲得本發明油墨’其於下文亦稱為 WF1.2。 II.施用本發明水性調配物WF1」或WF1.2及製造本發明 電極 所使用之載體(A.1)係一側面上已藉由(B.1)/(C·〗)混合物 塗覆之金屬網狀物。此經塗覆之金屬網狀物係與塗層一起 共400 μηι厚且具有90格利秒/1〇 之透氣性。 隨後,利用喷搶將本發明水性調配物WF. 1喷塗於具有 75 C溫度之真空工作台上,及使用氮氣於進行噴塗。此產 生基於(B.l)、(c.l)及(D.1)之總和計得為25 mg/cm2之負載 量0 接著利用具有以下壓延機設定值之壓延機進行壓延: 2 N/mm2之壓力 0.5 m/分鐘之前進速率 100°C之輥輪溫度 接著於溫度32CTC之烘箱中熱處理。於此溫度下,聚四氟 乙稀變軟。 此獲得本發明電極electr l。 ΠΙ.製造本發明電化學電池並測試 本發明電極展現1.35至1.5伏特之開路電勢。於放電期 156873.doc •25- 201228081 間’電池電壓於20 mA/cm2之放電電流下降低至1.2至1.25 伏特。於充電操作期間,電池電壓於2〇 mA/cm2之電流密 度下升咼至1.95至2.00 V之間之值。於較高電流密度(例 如,50 mA/cm2)下,放電期間之電壓為i丨至丨15伏特。就 充電操作而言,在50 mA/cm2之電流密度下觀察到2〇〇至 2·〇5 V之間之電壓。本發明電極在電化學測試電池(半電 池)中實現多於100個傭環。 156873.doc -26 -Cd-air battery pack, Fe_air battery pack, A1 air battery pack or zinc/air battery pack. The electrochemical cell of the present invention may have other components, for example, an outer shape, particularly a cylindrical, disc or rectangular parallelepiped casing, and at least one counter electrode. The opposite electrode contains as an essential component a metal in the form of an element 'for example, Fe, A, Cd or especially zinc. 156873.doc • 17- 201228081 The metal in elemental form may be a solid slab, a sintered porous electrode or a metal powder or The form of the pellets, which are sintered as needed. In one embodiment, the metal (especially zinc) is in the form of an element having a powder having an average particle diameter (average number of values) in the range of, for example, 2 μm to 500 μm, preferably 30 to 100 μm. In one embodiment, the metal in powder form is mixed with an organic binder to improve dimensional stability. Suitable organic binders are polysulfones, polyethersulfones and especially fluorinated (co)polymers such as polytetrafluoroethylene (pTFE) and polyvinylidene fluoride (PVDF). In a preferred embodiment, the metal in powder form, especially zinc in powder form, is used in combination with a paste or paste of an organic binder. The electrochemical cell of the present invention may further comprise at least one spacer that mechanically separates the electrically charged electrodes from one another, thereby preventing short circuits. Suitable spacer polymer films&apos; are in particular porous polymer films which are not reactive towards metals in elemental state and media which are generally strongly alkaline in the electrochemical cells of the invention. Particularly suitable materials for the spacer are polyolefins, especially porous polyethylene films and porous polypropylene films. Polycarbonate spacers, especially polyethylene or polypropylene spacers, may have from 35 to 45. Porosity in the range of /. A suitable pore size is, for example, in the range of 3 Å to 5 Å nm. In another embodiment of the invention, the spacer may be selected from PET nonwovens filled with alkali stabilized inorganic particles. These spacers may have a porosity in the range of 4 〇 to 55 〇 / 。. A suitable aperture system is, for example, in the range of 8 〇 to 75 〇 nm. 156873.doc 18·201228081 To fabricate an electrochemical cell of the present invention, the procedure can be, for example, combining the electrodes, spacers, and opposing electrodes of the present invention with one another and introducing them into a housing having any other components. The electrochemical cell of the present invention may further comprise at least one electrolyte which is a combination of at least one solvent and at least one type of salt compound or salt. Examples of suitable electrolytes are, in particular, aqueous alkaline solutions, for example sodium hydroxide solutions or hydroxide decompression solutions. In one embodiment of the invention, the electrochemical cell of the present invention may comprise another electrode, for example, as a reference electrode. Another suitable electrode is, for example, a zinc wire. The invention further provides a method of making the electrode of the invention, hereinafter also referred to as the method of manufacture of the invention. To practice the manufacturing method of the present invention, the procedure may be to (B) at least one electrically conductive carbonaceous material, (C) at least one organic polymer, and (D) at least one in particulate form and having from 1 to 3 〇〇m2/g The compound of formula (I) having a BET surface area in the range is applied in one or more steps to (A) a solid medium through which the gas can diffuse. The procedure may specifically be as follows: (B) at least one electrically conductive carbonaceous material (C) at least one organic polymer and (D) at least one in particulate form and having a BET surface area in the range of from 1 to 3 〇〇 m 2 /g The compound of the formula (I) 156873.doc • 19·201228081 is applied in the form of an aqueous or solvent-based ink or a preferred aqueous paste or preferably an aqueous paste to (A) a solid medium through which the gas can diffuse. The compound of formula (I) is as described above. The remaining variables are also as described above. Compound (D) (e.g., coating) may also be treated first with conductive carbon (B), and then mixed with polymer (C) and applied to carrier (a). For example, the coating can be applied by spraying (e.g., spraying or misting) and knife coating, printing, or by pressing. In the context of the present invention, the spray also includes application by squirting. This method is often also referred to as "air brushing" or simply "airbrushing". The manufacturing process of the present invention is, for example, from one or more compounds (d). For example, compound (D) can be prepared by mixing suitable compounds of (4) and/or m4 as needed, for example, in dry form or as a solution or suspension. Preferably, according to the stoichiometry of Μ1, Μ, Μ and Μ# in the compound (D), the ratio of the compound to the desired compound is selected. The mixture obtained in this way is then passed through a heat; for example, the pot can be calcined, for example, at a temperature of from 250 to, preferably in the range of just t: the calcination can be carried out in an inert gas or in an oxidizing atmosphere, for example Air (or another mixture of inert gas and oxygen) is carried out. The calcination time can range from a few minutes to a few hours. Suitable starting materials which can be used to make the compound (9) include oxides, gas oxides or base oxides of μ1, yttrium, W and MW. Other such compounds which may be used, M, M2, M3 and/or M4, are present in the presence of oxygen or in the presence of 156873.doc 201228081 due to the heating reaction to produce oxides, hydroxides or base oxides. Compound (D) can be prepared by mixing the starting materials in a dry or wet form. If it is to be carried out in a dry form, the starting material for the preparation of the compound (D) can be used in the form of a fine powder, and after calcination and, if necessary, calcination. However, it is preferred to carry out intimate mixing in a wet form. In general, this involves mixing the starting materials f used to prepare the compound (D) with each other in the form of an aqueous solution and/or a suspension. The starting of the preparation of the compound (D) can be obtained by starting from the compound of M丨, M2, M3 and/or Μ# in a dissolved form and precipitating a compound of ruthenium, osmium, M3 and/or μ4. A very good mixture of substances. The aqueous material obtainable therefrom is then dried in an excellent drying manner at a temperature in the range of preferably from 1 (10) to 15 (rc), and is spray dried, especially at an outlet temperature in the range of (10) to thief. The step of establishing the desired particle size of the compound (9) may be carried out before, during or after the heat treatment, for example, screening, grinding or grading. In the optional step, the ruthenium is treated with conductive carbon (8) (9), for example, coated. () To carry out this treatment, for example, the compound (D) can be sufficiently blended with the conductive carbon (B), for example, if it is ground. For example, a grinder, especially a ball mill, is suitable for grinding. In another variation in which the compound (D) is treated by conductive carbon (8) as needed, carbon may be deposited on the compound (D), for example, by decomposing an organic compound. This is then mixed with polymer (C) which can be added, for example, in the form of an aqueous dispersion or pellet. 156873.doc -21- 201228081 In another embodiment, compound (D), conductive carbon (B) may be mixed in one step, for example, by stirring the corresponding solid with one or more organic solvents or with water as needed. And polymer (C) wherein polymer (c) can be added, for example, in the form of an aqueous dispersion or pellet. As the mixing, for example, a stirring device such as a stirring tank or a grinder (for example, a ball mill and especially an agitating ball mill) can be used. In other embodiments, ultrasonic waves are used, for example, by means of a sonotrode. This results in a preferred aqueous formulation. Subsequently, the desired properties of the preferred aqueous formulation to be applied, such as viscosity or solids content, are determined. In the present invention, these preferred aqueous formulations having a solids content in the range of 0.5 to 25% are referred to as inks. These preferred aqueous formulations having a solids content greater than 25% are referred to as pastes. In one embodiment of the invention, the preferred aqueous formulation comprises at least one surfactant. In the context of the present invention, the surfactant is a surface active substance. The surfactant may be selected from the group consisting of cationic, anionic and preferably nonionic surfactants. Subsequent length 1 supply; quality (A) or carrier (A), and preferably aqueous formulation or comprising conductive carbon (B), polymer (c), compound (D) and any discharge catalyst (E) Preferred aqueous formulations are applied to the medium (a) or carrier (4) in one or more steps. This application can be carried out, for example, by dusting, spraying (especially by spraying), and by knife coating or preferably printing. In another embodiment of the present invention, the solvent-free conductive carbon (B) poly-sigma (C) can be, for example, at a pressure in the range of 3 Torr to 3 Torr and a temperature in the range of 150 to 320 C. , compound (D) and optionally discharge catalyst (E) component 156873.doc -22- 201228081 The mixture is compressed with each other. For this purpose, it can be self-paste, preferably starting from an aqueous paste, the layer height of which can be adjusted to the desired size by means of rolling and cutting, and applied to the medium of interest (A) . After application, it can be followed, for example, by heat treatment, especially at 15 to 35 Torr. (: is fixed at a temperature within the range, especially at a temperature close to the glass transition temperature of the polymer (c). In this case, for example, when a vinylidene fluoride-hexafluoropropylene copolymer is selected as the polymer ( In the case of c), it is preferred to select the temperature, for example, in the range of from 125 to 175 C, preferably about i5 Torr. In another variation, the temperature selected is from 175 to 225^, preferably about 2 〇. (rc, and the selected polymer (C) is polyvinylidene fluoride. In another variation, the temperature selected is 300 to 350 C', preferably 320 to 325 ° C, and the selected polymer (C) Polytetrafluoroethylene. In a variant, it can be fixed mechanically, for example by calendering. This is an electrode of the invention which can be combined with other components to form the electrochemical cell of the invention. This has excellent overall properties. An electrochemical cell of the present invention. Another aspect of the invention is a formulation, also referred to as a formulation of the invention, comprising at least one organic solvent or water and (B) at least one electrically conductive carbonaceous material; (C) at least one Organic polymer and (D) at least one comprising molybdenum or tungsten A mixed oxide of at least one element selected from the group consisting of Fe, Ag, a lanthanide metal, and V. An aqueous formulation is preferred. Conductive carbon (ruthenium), polymer (C), and compound (D) have been defined above. .doc • 23-201228081 In a preferred embodiment of the present invention, the preferred aqueous formulation of the present invention comprises at least one other component selected from the group consisting of surfactants, thickeners, and antifoaming agents. The preferred aqueous formulation of the present invention may have a solids content in the range of from 0.5 to 60%. The invention is illustrated by the working examples. Basic Remarks: In the context of the present invention, the numbers are expressed as percentages unless otherwise explicitly stated. Refers to the weight percentage. I. Manufacture of aqueous formulation 1.1 Manufacture of aqueous ink, WF1.1 In a stirred vessel, mix 2 g of ethoxylated trimethyldecyl alcohol and 66.5 g of water using a magnetic stirrer. 4 g Nis, 〇4 gw〇^ig FeAgM〇2〇8 (D.1) (BET surface area 1 5 m2/g) and 3 g Ag activated carbon (9% Ag coating (Β·υ, while stirring. Use ultrasonic waves to be dispersed by the following procedure: 14 mm US sonic pole, loop owing, vibration 45% ' 8. Cooling, magnetic stirrer 75 〇 /. 'Enlarged energy input of 0.025 kWh. Then add 3.8 g of aqueous dispersion of polytetrafluoroethylene (ci) with 60% solids content, and: no further The mixture was stirred for 15 minutes under ultrasound. The ink of the invention was obtained by filtering the mixture through a 19 pm mesh screen, which is also referred to below as WF 1.1. 1.2 Manufacture of aqueous ink, WF 1.2 in a stirred vessel, using a magnetic force Agitator was used to mix 2 g of ethoxylated dimethyl decyl alcohol and 66.5 g of water. Subsequently, 〇4 g Nis, 〇4 g WC and 0.4 g Fe2(W04)3(D.2) (BET surface area 3 m2/g) and 3 g^active stone anaesthesia (9〇/〇Ag coating C) were added (B 1), while mixing. Subsequent use of ultrasonic waves by 156873.doc -24· 201228081 under the program: 14 mm US sound pole, cycle 1 time, amplitude 45% ' 8 ° C cooling 'magnetic stirrer 75%, up to 0.025 kWh energy input . Subsequently, 3.8 g of an aqueous dispersion of polytetrafluoroethylene (C1) having a solid content of 60% was added, and the mixture was stirred for 15 minutes without further ultrasonication. The ink of the present invention was obtained by filtering the mixture through a 19 Å μηι sieve, which is also referred to as WF1.2 hereinafter. II. Application of the aqueous formulation WF1" or WF1.2 of the present invention and the carrier (A.1) used for the manufacture of the electrode of the invention are coated on one side by a mixture of (B.1)/(C·) Metal mesh. The coated metal mesh is 400 μηι thick with the coating and has a gas permeability of 90 Gilliseconds/1 Torr. Subsequently, the aqueous formulation WF. 1 of the present invention was sprayed on a vacuum table having a temperature of 75 C by means of spray blasting, and spraying was carried out using nitrogen gas. This yields a loading of 25 mg/cm2 based on the sum of (Bl), (cl) and (D.1). Then the calendering is carried out using a calender with the following calender settings: 2 N/mm2 pressure 0.5 The roll temperature of 100 ° C before the m/min is then heat treated in an oven at a temperature of 32 CTC. At this temperature, the polytetrafluoroethylene becomes soft. This obtains the electrode electr l of the present invention.制造. The electrochemical cell of the present invention was fabricated and tested. The electrode of the present invention exhibited an open circuit potential of 1.35 to 1.5 volts. During the discharge period 156873.doc •25- 201228081' battery voltage is reduced to 1.2 to 1.25 volts at a discharge current of 20 mA/cm2. During the charging operation, the battery voltage is ramped up to a value between 1.95 and 2.00 V at a current density of 2 mA/cm2. At higher current densities (e.g., 50 mA/cm2), the voltage during discharge is i丨 to 丨15 volts. For the charging operation, a voltage between 2 〇〇 and 2·〇 5 V was observed at a current density of 50 mA/cm 2 . The electrode of the present invention achieves more than 100 commission rings in an electrochemical test cell (semi-battery). 156873.doc -26 -

Claims (1)

201228081 七、申請專利範圍: 1· 一種電極’其包含: (A) 氣體可擴散通過之固體介質, (B) 至少一種導電碳質材料, ’ (C)至少一種有機聚合物, . (D)至少一種呈顆粒形式之通式⑴之化合物 M1aM1bM2cM3dHeOf (I) 其中該等變數各定義如下: 係選自 Mo、W、V、Nb及 Sb, Μ1係選自Fe、Ag、Cu、Ni、Μη及鑭系金屬, M 係選自 B、C、N ' A1、Si、P及 Sn, M 係選自 Li、Na、K、Rb、Cs、NH4、Mg、Ca及 Sr, a 係於1至3之範圍内, b 係於〇·1至10之範圍内, c 係於〇至1之範圍内, d 係於0至1之範圍内, 6 係於〇至5之範圍内, f 係於1至28之範圍内, • 及其中該通式⑴之化合物具有在1至300 m1/g範圍内之 . BET表面積。 1 ·如凊求項1之電極,其中該化合物(D)係選自混合氧化物 及異多元酸及其鹽。 2 士明求項1或2之電極’其中該化合物(D)係選自卩6_八经_父_ 〇、Fe-V-X·0、Ag-X-V-0、Ce-X-O及 Fe-X-O,其中 X係 3 156873.doc 201228081 選自鉬及瑪β 4. 如咕求項1或2之電極,其中該有機聚合物(c)係選自鹵化 (共)聚合物。 5. 如凊求項1或2之電極,其中該固體介質(A)係選自金屬網 狀物及由碳構成之氣體擴散介質。 6. 如响求項1或2之電極,其中該導電碳質材料(B)具有在20 至1500 m2/g範圍内之BET表面積。 7. 如请求項1或2之電極,其中該化合物(D)具有在1〇至5〇 nm範圍内之平均初級粒徑。 8. 如。月求項1或2之電極’其中該化合物⑼係呈聚結顆粒之 t式°亥專聚結物具有20 nm至50 μιη之平均直徑。 9. 如吻求項1或2之電極,其進一步包含放電觸媒。 10. 種如3月求項1至9中任一項之電極於電化學電池中之用 途。 11. 如清求項10之用途,其中該等電化學電池包含鎘·空氣電 池組、鋁_空氣電池組、鐵-空氣電池組或辞-空氣電池 組。 12. —種電化學電池,其包含至少一個如請求項1至9中任— 項之電極。 13· —種利用如請求項12之電化學電池操作設備之方法。 14. 一種製造如請求項!至9中任一項之電極之方法,其包 含將 ' (B) 至少一種導電碳質材料, (C) 至少一種有機聚合物,及 156873.doc 201228081 (D)至少一種呈顆粒形式且具有在1至3〇〇 m2/gi圍内之 BET表面積之通式(I)之化合物 以一或多個步驟施用至 (A) 氣體可擴散通過之固體介質。 15. 如請求項14之方法,其中 (B) 至少一種導電碳質材料, (C) 至少一種有機聚合物及 (D) 至少一種呈顆粒形式且具有在1至3〇〇 m2/gs圍内之 BET表面積之通式⑴之化合物 係以油墨或糊料或膠糊之形式施用至 (A) 氣體可擴散通過之固體介質。 16. 如請求項14及15中任一項之方法,其中該施用後接著熱 處理。 17 · —種調配物,其包含至少一種有機溶劑或水及 (B) 至少一種導電碳質材料, (C) 至少一種有機聚合物,及 (D) 至少一種呈顆粒形式之通式⑴之化合物 M1aM2bM3cM4dHeOf (I) 其中S玄等變數各定義如下: M1 係選自 Mo、W、V、Nb及 Sb, Μ2係選自pe、Ag、Cu、Ni、Μη及鑭系金屬, M 係選自 Β、C、Ν、A1、Si、Ρ及 Sn ’ Μ 係選自 Li、Na、K、Rb、Cs、NH4、Mg、Ca及 Sr, 156873.doc 201228081 a 係於1至3之範圍内, b 係於0.1至10之範圍内, c 係於0至1之範圍内, d 係於0至1之範圍内, e 係於0至5之範圍内, f 係於1至28之範圍内, 及其中該通式(I)之化合物具有在1至300 m2/g範圍内之 BET表面積。 156873.doc 201228081 四、指定代表圖: (一) 本案指定代表圖為:(無) (二) 本代表圖之元件符號簡單說明: 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: (無) 156873.doc201228081 VII. Patent application scope: 1. An electrode comprising: (A) a solid medium through which a gas can diffuse, (B) at least one conductive carbonaceous material, '(C) at least one organic polymer, (D) At least one compound of the formula (1) M1aM1bM2cM3dHeOf (I) in the form of particles, wherein the variables are defined as follows: selected from the group consisting of Mo, W, V, Nb and Sb, and the lanthanum 1 is selected from the group consisting of Fe, Ag, Cu, Ni, Μ and Lanthanide metal, M is selected from the group consisting of B, C, N ' A1, Si, P and Sn, and M is selected from the group consisting of Li, Na, K, Rb, Cs, NH4, Mg, Ca and Sr, a is from 1 to 3 Within the range, b is in the range of 〇·1 to 10, c is in the range of 〇1, d is in the range of 0 to 1, 6 is in the range of 〇5, and f is in the range 1. Within the range of 28, and the compound of the formula (1) has a BET surface area in the range of 1 to 300 m1/g. An electrode according to claim 1, wherein the compound (D) is selected from the group consisting of mixed oxides and isopolyacids and salts thereof. 2 The electrode of claim 1 or 2 wherein the compound (D) is selected from the group consisting of 卩6_八经_父_〇, Fe-VX·0, Ag-XV-0, Ce-XO and Fe-XO, Wherein X system 3 156873.doc 201228081 is selected from the group consisting of molybdenum and gamma β 4. The electrode of claim 1 or 2, wherein the organic polymer (c) is selected from a halogenated (co)polymer. 5. The electrode of claim 1 or 2, wherein the solid medium (A) is selected from the group consisting of a metal mesh and a gas diffusion medium composed of carbon. 6. The electrode of claim 1 or 2, wherein the electrically conductive carbonaceous material (B) has a BET surface area in the range of from 20 to 1500 m2/g. 7. The electrode of claim 1 or 2, wherein the compound (D) has an average primary particle size in the range of 1 〇 to 5 〇 nm. 8. For example. The electrode of the first or second item, wherein the compound (9) is a coalesced particle, has a mean diameter of from 20 nm to 50 μm. 9. The electrode of claim 1 or 2, further comprising a discharge catalyst. 10. The use of an electrode according to any one of items 1 to 9 of March in an electrochemical cell. 11. The use of claim 10, wherein the electrochemical cells comprise a cadmium/air battery, an aluminum-air battery, an iron-air battery, or a speech-air battery. 12. An electrochemical cell comprising at least one electrode as claimed in any one of claims 1 to 9. 13. A method of operating an apparatus using an electrochemical cell as claimed in claim 12. 14. A manufacturing as requested! The method of any of the electrodes of any one of the preceding claims, comprising: (B) at least one electrically conductive carbonaceous material, (C) at least one organic polymer, and 156873.doc 201228081 (D) at least one in particulate form and having The compound of formula (I) having a BET surface area in the range of from 1 to 3 〇〇 m 2 / gi is applied in one or more steps to (A) a solid medium through which the gas can diffuse. 15. The method of claim 14, wherein (B) at least one electrically conductive carbonaceous material, (C) at least one organic polymer, and (D) at least one in particulate form and having a range of from 1 to 3 〇〇 m2/gs The compound of the formula (1) having a BET surface area is applied in the form of an ink or a paste or a paste to (A) a solid medium through which a gas can diffuse. 16. The method of any of claims 14 and 15, wherein the applying is followed by heat treatment. a formulation comprising at least one organic solvent or water and (B) at least one electrically conductive carbonaceous material, (C) at least one organic polymer, and (D) at least one compound of the formula (1) in particulate form M1aM2bM3cM4dHeOf (I) wherein the S-equivalent variables are defined as follows: M1 is selected from the group consisting of Mo, W, V, Nb and Sb, and Μ2 is selected from the group consisting of pe, Ag, Cu, Ni, Μ and lanthanide metals, and M is selected from Β. , C, Ν, A1, Si, Ρ and Sn ' Μ are selected from the group consisting of Li, Na, K, Rb, Cs, NH4, Mg, Ca and Sr, 156873.doc 201228081 a is in the range of 1 to 3, b In the range of 0.1 to 10, c is in the range of 0 to 1, d is in the range of 0 to 1, e is in the range of 0 to 5, f is in the range of 1 to 28, and Wherein the compound of the formula (I) has a BET surface area in the range from 1 to 300 m2/g. 156873.doc 201228081 IV. Designated representative map: (1) The representative representative of the case is: (none) (2) The symbol of the symbol of the representative figure is simple: 5. If there is a chemical formula in this case, please reveal the best indication of the characteristics of the invention. Chemical formula: (none) 156873.doc
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