TWI700852B - Electrode for battery and biochemical fuel cell - Google Patents
Electrode for battery and biochemical fuel cell Download PDFInfo
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- TWI700852B TWI700852B TW105110242A TW105110242A TWI700852B TW I700852 B TWI700852 B TW I700852B TW 105110242 A TW105110242 A TW 105110242A TW 105110242 A TW105110242 A TW 105110242A TW I700852 B TWI700852 B TW I700852B
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- 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
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/05—Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/16—Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/133—Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
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- 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
- Y02E60/10—Energy storage using batteries
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- 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
Abstract
本發明提供一種可更提升輸出的電池用電極及生化燃料電池。 The present invention provides a battery electrode and a biochemical fuel cell that can increase the output.
本發明的電池用電極1包括:經疊合複數個碳纖維3而形成3維網狀構造的骨架2;於複數個碳纖維3的表面所形成的碳奈米管構造體5,該碳奈米管構造體5為由複數個碳奈米管6形成彼此直接連接的網絡構造,並直接固定於碳纖維3表面,由於骨架2無須透過接著劑黏聚,故,亦不會阻礙電解液流通,又,可增加電池用電極的比表面積,且碳奈米管未透過絕緣體而是直接固定在碳纖維3,故較以往可更抑制電池用電極的電阻增加,在應用於電池中時,可更提升電池的輸出。 The battery electrode 1 of the present invention includes: a skeleton 2 formed by laminating a plurality of carbon fibers 3 to form a three-dimensional network structure; a carbon nanotube structure 5 formed on the surface of the plurality of carbon fibers 3, the carbon nanotube The structure 5 is a network structure formed by a plurality of carbon nanotubes 6 directly connected to each other, and is directly fixed to the surface of the carbon fiber 3. Since the skeleton 2 does not need to be cohesive through an adhesive, it does not hinder the flow of electrolyte. The specific surface area of the battery electrode can be increased, and the carbon nanotube is directly fixed to the carbon fiber 3 without penetrating the insulator. Therefore, the resistance increase of the battery electrode can be suppressed more than before. When applied to the battery, the battery's performance can be improved. Output.
Description
本發明關於一種電池用電極及生化燃料電池。 The invention relates to an electrode for a battery and a biochemical fuel cell.
近年來,作為將酵素用於觸媒取代白金等金屬觸媒的燃料電池的生化燃料電池正受到矚目。生化燃料電池係利用氧化還原酵素,使燃料氧化及氧還原,將化學能轉變成電能。 In recent years, biochemical fuel cells have attracted attention as fuel cells that use enzymes as catalysts instead of metal catalysts such as platinum. The biochemical fuel cell system uses redox enzymes to oxidize fuel and reduce oxygen to convert chemical energy into electrical energy.
為了提升此種生化燃料電池之輸出,進行各種改良。 In order to increase the output of this biochemical fuel cell, various improvements have been made.
例如,於專利文獻1中所揭示一種將氧化鋯與科琴黑(Ketjenblack,亦稱超導碳黑),以聚四氟乙烯(PTFE)結著於碳纖布上,增加電極的比表面積的電極。
For example,
【先前技術文獻】 【Prior Technical Literature】
專利文獻 Patent literature
專利文獻1:日本特開2012-28181號公報 Patent Document 1: Japanese Patent Application Publication No. 2012-28181
然而,專利文獻1中所揭示的電極中,作為接著劑的PTFE堵塞於碳纖布的細孔中,碳纖布因PTFE而黏聚,在用於生化燃料電池的電極時,阻礙電解液的流通,有生化燃
料電池的輸出難以提升的問題。
However, in the electrode disclosed in
此外,專利文獻1中所揭示的電極,雖然因碳纖布上附著有科琴黑而使比表面積增大,然而,科琴黑與碳纖布以透過絕緣體PTFE而固定,科琴黑與碳纖布之間的電阻變高,用於作為生化燃料電池的電極時,生化燃料電池的內部電阻變高,有生化燃料電池的輸出難以提升的問題。
In addition, the electrode disclosed in
在此,本發明的目的為提供一種可更提升輸出的電池用電極及生化燃料電池。 Here, the object of the present invention is to provide a battery electrode and a biochemical fuel cell that can further increase the output.
本發明的電池用電極係包括:經疊合複數個碳纖維而形成3維網狀構造的骨架;於複數個上述碳纖維的表面所形成的碳奈米管構造體,上述碳奈米管構造體為由複數個碳奈米管形成彼此直接連接的網絡構造,並直接固定於上述碳纖維表面。 The battery electrode system of the present invention includes: a skeleton formed by laminating a plurality of carbon fibers to form a three-dimensional network structure; a carbon nanotube structure formed on the surface of the plurality of carbon fibers, the carbon nanotube structure being A plurality of carbon nanotubes form a network structure directly connected to each other and are directly fixed on the surface of the carbon fiber.
本發明的生化燃料電池係使用申請專利範圍第1~7項中任一項所述的電池用電極。
The biochemical fuel cell of the present invention uses the battery electrode described in any one of
本發明的電池用電極,其3維網狀構造的骨架無須透過接著劑黏聚,故不會阻礙電解液的流通,又,可增加電池用電極的比表面積,且碳奈米管未透過絕緣體而是直接固定於碳纖維,因此,可較以往更抑制電池用電極的電阻的增加,應用於電池時,可更提升電池的輸出。 In the battery electrode of the present invention, the skeleton of the three-dimensional network structure does not need to be cohesive through the adhesive, so it does not hinder the flow of electrolyte, and can increase the specific surface area of the battery electrode, and the carbon nanotube does not penetrate the insulator It is directly fixed to the carbon fiber, so the increase in the resistance of the battery electrode can be suppressed more than before, and when applied to a battery, the output of the battery can be improved.
本發明的生化燃料電池,由於未阻礙電解液的流通,可較以往更有效率地產生電能,又,由於電池用電極的比 表面積增大,可較以往更增加電流密度,故可更提升電池的輸出。 Since the biochemical fuel cell of the present invention does not hinder the flow of electrolyte, it can generate electric energy more efficiently than before. In addition, due to the comparison of battery electrodes The increased surface area can increase the current density more than before, so the output of the battery can be improved.
1‧‧‧電池用電極 1‧‧‧Electrode for battery
2‧‧‧骨架 2‧‧‧Frame
3‧‧‧碳纖維 3‧‧‧Carbon Fiber
4‧‧‧連接部 4‧‧‧Connecting part
5‧‧‧碳奈米管構造體 5‧‧‧Carbon Nanotube Structure
6‧‧‧碳奈米管 6‧‧‧Carbon Nanotube
第1圖係放大表示電池用電極的一部的示意圖。 Fig. 1 is a schematic diagram showing an enlarged part of a battery electrode.
第2圖係拍攝電池用電極的表面的SEM圖像。 Fig. 2 is an SEM image of the surface of the battery electrode.
第3A圖係放大表示電池用電極的碳纖維的SEM圖像。 Fig. 3A is an enlarged SEM image showing the carbon fiber of the battery electrode.
第3B圖更放大表示電池用電極的碳纖維的SEM圖像。 Figure 3B shows a more enlarged SEM image of the carbon fiber of the battery electrode.
(1)本實施形態的生化燃料電池 (1) Biochemical fuel cell of this embodiment
關於本實施形態的生化燃料電池,作為陽極電極及陰極電極,除了使用下述本實施形態的電池用電極以外,其餘可使用習知的生化燃料電池的構成。 Regarding the biochemical fuel cell of this embodiment, as the anode electrode and the cathode electrode, except for the battery electrode of this embodiment described below, a conventional biochemical fuel cell configuration can be used.
例如,本實施形態的生化燃料電池具有將陽極電極及陰極電極配置於電解液中的構成。電解液中包含經氧化放出電子的燃料;於陽極電極使燃料氧化,同時於陰極電極使氧等還原的氧化還原酵素;媒介酵素及電極之間電子的傳遞的電子傳遞介質。 For example, the biochemical fuel cell of this embodiment has a configuration in which the anode electrode and the cathode electrode are arranged in an electrolyte. The electrolyte contains a fuel that emits electrons through oxidation; a redox enzyme that oxidizes the fuel at the anode electrode and reduces oxygen at the cathode electrode; an electron transfer medium that mediates the transfer of electrons between the enzyme and the electrode.
作為燃料,可使用糖、醇類、有機酸、胺類、氫及無機化合物等生物可作為能量源利用全部的還原物質。 As fuels, sugars, alcohols, organic acids, amines, hydrogen, and inorganic compounds can be used as energy sources and all reducing substances can be used.
更具體而言,作為燃料,可使用甲醇、乙醇、丙醇、甘油、聚乙烯醇等醇類;葡萄糖、果糖、山梨糖等醣類;甲醛、乙醛等醛類;以及此等的混合物。 More specifically, as the fuel, alcohols such as methanol, ethanol, propanol, glycerin, and polyvinyl alcohol; sugars such as glucose, fructose, and sorbose; aldehydes such as formaldehyde and acetaldehyde; and mixtures thereof can be used.
作為氧化還原酵素,可使用可使上述燃料氧化, 使氧還原的酵素,對應所使用的燃料選擇即可。 As a redox enzyme, it can be used to oxidize the above fuel, The enzyme that reduces oxygen can be selected according to the fuel used.
例如,作為氧化還原酵素,可使用漆酶(laccase)、抗壞血酸氧化酶、膽紅素酶(BOD)、葡萄糖脫氫酶(GDH)、乙醇脫氫酶(ADH)、醛脫氫酶、葡萄糖氧化酶(GOD)、醇氧化酶(AOD)、及醛氧化酶等。 For example, as redox enzymes, laccase (laccase), ascorbate oxidase, bilirubinase (BOD), glucose dehydrogenase (GDH), alcohol dehydrogenase (ADH), aldehyde dehydrogenase, glucose oxidation can be used Enzyme (GOD), alcohol oxidase (AOD), and aldehyde oxidase, etc.
氧化還原酵素可僅單獨使用1種,亦可組合2種以上使用。 Redox enzymes may be used alone or in combination of two or more kinds.
作為電子傳遞介質,例如可使用以Os、Fe、Ru、Co、Cu、Ni、V、Mo、Cr、Mn、Pt及W等金屬元素作為中心金屬的金屬錯合物;醌、苯醌、蔥醌及萘醌等醌類;紫精(viologen)、甲基紫精及苄基紫精等雜環式化合物等。電子傳遞介質可對應所使用的氧化還原酵素而選擇。又,以使用電子傳遞介質為佳,但不使用亦可。 As the electron transfer medium, for example, metal complexes with metal elements such as Os, Fe, Ru, Co, Cu, Ni, V, Mo, Cr, Mn, Pt, and W as the central metal can be used; quinone, benzoquinone, onion Quinones and naphthoquinones; heterocyclic compounds such as viologen, methyl viologen and benzyl viologen. The electron transfer medium can be selected according to the redox enzyme used. In addition, it is better to use an electronic transfer medium, but it may not be used.
(2)本實施形態的電池用電極的構成 (2) The structure of the battery electrode of this embodiment
如第1圖所示,電池用電極1包括:骨架2、形成於骨架2表面的碳奈米管(以下,稱為CNT)構造體5。骨架2具有:複數個碳纖維3、連接碳纖維3彼此的連接部4,形成將複數個碳纖維3疊合而成的3維網狀構造。實際上,電池用電極1為板狀,但為了說明上的方便,第1圖將電池用電極1的一部份放大表示。
As shown in FIG. 1, the
骨架2係由彼此交纏的複數個碳纖維3接觸的部份、相鄰碳纖維3彼此接觸的部份、以及複數個碳纖維3形成的網目等當中的一部份,以樹脂等接著劑形成的連接部4所形成,碳纖維3彼此以連接部4連接。
The
本實施形態的情形,連接部4經碳化而具有導電性。故,骨架2相較於連接部4以樹脂等絕緣體形成時,導電性較高。連接部4例如由Teflon(註冊商標)等形成的樹脂組成物附著於骨架2,以此種狀態使該樹脂組成物經碳化而形成。
In the case of this embodiment, the connecting
骨架2並不限於以碳纖維所形成的3維網狀構造,亦可不具有連接部4。作為骨架2,例如可使用市售的碳紙、碳不織布及碳纖布等。本實施形態的情形,骨架2為碳紙。
The
此外,本實施形態的情形,形成骨架2的碳纖維3及連接部4的表面經氧化,於碳纖維3及連接部4的表面的一部份形成羥基及羧基等官能基。
In addition, in the case of this embodiment, the surfaces of the
於形成骨架2的碳纖維3的表面形成CNT構造體5。CNT構造體5包含均勻地分散的複數個CNT6。複數個CNT6彼此直接連接,形成網絡構造。此處的直接連接係指CNT6彼此未以分散劑或界面活性劑、接著劑等覆蓋,彼此纏繞的狀態,亦即CNT6彼此之間未透過接著劑或分散劑、界面活性劑等媒介物而連接,包含物理性的連接(單純的接觸)、化學性的連接。此種CNT構造體5亦形成於連接部4的表面。
A
CNT構造體5以平均厚度500nm以下為佳。當CNT構造體5的平均厚度超過500nm時,覆蓋碳纖維3表面的CNT構造體5變得過多。如此一來CNT6凝聚的比例變高造成電性導電性或熱傳導性降低,且限制CNT構造體5來自碳纖維3的機能。此外,電池用電極1作為生化燃料電池的電極使用時,
阻礙電解液或氧化還原酵素等的流通,有電池的輸出性能降低的疑慮。
The
且,CNT構造體5的平均厚度依比較CNT構造體5形成前與形成後的碳纖維3的掃瞄式電子顯微鏡(Scanning Electron Microscope:SEM)圖像而測定。具體而言,首先,於CNT構造體5形成前的碳纖維3的SEM圖像中30處,測定CNT構造體5形成前的碳纖維3的徑,計算出CNT構造體5形成前的碳纖維3的平均徑。接著,於CNT構造體5形成後的碳纖維3的SEM圖像中的30處,測定CNT構造體5形成後的碳纖維3的徑,計算出CNT構造體5形成後的碳纖維3的平均徑。最後,由CNT構造體5形成後的碳纖維3的平均徑中扣除CNT構造體5形成前的碳纖維3的平均徑,計算出CNT構造體5的平均厚度。
In addition, the average thickness of the
CNT構造體5的平均厚度以5nm以上100nm以下為更佳。只要CNT構造體5的厚度在上述範圍內,CNT6分散於碳纖維3表面,彼此直接連接可形成良好的CNT6的網絡構造。此處的網絡構造並不限於在碳纖維3表面形成全體成為一個網絡的情形,亦包含複數個網絡構造獨立存在的構造,複數個網絡構造部份直接連接的構造,一碳纖維3表面的網絡構造與其他碳纖維3或連接部4的表面的網絡構造部份直接連接的構造。
The average thickness of the
CNT6以多層為佳。又,CNT6以長度為0.1μm以上50μm以下為佳。當CNT6長度為0.1μm以上時,CNT6彼此纏繞而直接連接。又,當CNT6長度為50μm以下時,容易 均勻地分散。另一方面,當CNT6長度未達0.1μm時,CNT6彼此變得不易纏繞。又,當CNT6長度超過50μm時,變得容易凝聚。 CNT6 is preferably multilayered. In addition, the length of CNT6 is preferably 0.1 μm or more and 50 μm or less. When the length of CNT6 is 0.1 μm or more, CNT6 is entangled with each other and directly connected. Also, when the length of CNT6 is 50μm or less, it is easy to Disperse evenly. On the other hand, when the length of CNT6 is less than 0.1 μm, it becomes difficult for CNT6 to be entangled with each other. In addition, when the length of CNT6 exceeds 50 μm, it becomes easy to aggregate.
CNT6以直徑為30nm以下較佳。CNT6直徑為30nm以下時,富有柔軟性,沿著碳纖維3或表面的曲率形變,容易形成網絡構造。另一方面,CNT6直徑超過30nm時,變得無柔軟性,不易沿著碳纖維3表面形變,因此難以形成網絡構造。
CNT6 preferably has a diameter of 30 nm or less. When the diameter of CNT6 is 30nm or less, it is rich in flexibility, deforms along the curvature of the
CNT6的直徑以20nm以下為更佳。且,將CNT6的直徑在依以下說明的方法將CNT6附著於碳纖維3前,取出一部份用於附著的CNT6,以穿透式電子顯微鏡(TEM:Transmission Electron Microscope)拍攝CNT6,使用拍攝的圖像作為測定的平均直徑。
The diameter of CNT6 is more preferably 20 nm or less. Also, before attaching the CNT6 to the
此外,CNT6的表面經氧化,於CNT6表面的一部份形成羥基及羧基等官能基。藉由於CNT6表面形成羥基或羧基,電池用電極1應用於電池的電極時,在電極的活性物質等的電子傳遞以透過羥基或羧基的方式而進行,電子的傳遞變得更平順地進行。結果,使用電池用電極1於電極的電池,可有效率地產生電能,提升電池的輸出。電池用電極1用於生化燃料電池的電極時,CNT6與電子傳遞介質之間電子的傳遞透過羥基或羧基進行,電子的傳遞變得更平順,更提升電池的輸出。
In addition, the surface of CNT6 is oxidized to form functional groups such as hydroxyl and carboxyl on a part of the surface of CNT6. Since a hydroxyl group or a carboxyl group is formed on the surface of CNT6, when the
此種所構成的CNT6,相對於骨架2,以0.001wt%以上2wt%以下的比例,固定於碳纖維3及連接部4的表面為
佳。CNT6以上述範圍內的比例時,於碳纖維3表面形成未覆蓋有CNT6的部份。此等未覆蓋有CNT6的部份,未覆蓋有接著劑等,暴露出碳纖維3的表面。藉此,骨架2不會損害CNT6具有的機能。CNT6的比例,相對於骨架2,以0.005wt%以上1wt%以下為佳,以0.01wt%以上0.1wt%以下更佳。
The CNT6 constructed in this way is fixed on the surface of the
此種CNT構造體5直接固定於碳纖維3的表面。換言之,CNT6既非於碳纖維3的表面,同時以接著劑或分散劑、界面活性劑等覆蓋而固定於碳纖維3的表面,亦非透過接著劑或分散劑、界面活性劑等而固定於碳纖維3,而是直接固定於碳纖維3的表面。此處固定係包含以几得瓦爾力界合碳纖維3與CNT6、透過形成於碳纖維3表面的羥基或羧基使碳纖維3與CNT6化學鍵結、及透過形成於CNT6表面的羥基或羧基使碳纖維3與CNT6化學鍵結。
Such a
此外,CNT構造體5同樣亦直接固定於連接部4的表面。並且,只要不限制骨架2及CNT6的機能,電池用電極1亦可包含碳纖維3及透過接著劑或分散劑等結合的CNT6。
In addition, the
(3)本實施形態的電池用電極的製造方法 (3) Manufacturing method of battery electrode of this embodiment
接著,說明電池用電極1的製造方法。電池用電極1係由(3-1)CNT製作步驟、(3-2)使用製作的CNT而生成CNT分散液的步驟、(3-3)使用CNT分散液於碳纖維表面形成CNT構造體的步驟而成。以下,依序說明關於各步驟。
Next, the manufacturing method of the
(3-1)CNT製作步驟 (3-1) CNT production steps
CNT6例如可使用日本特開2007-126311號公報所記載的熱CVD法製作。以此情況、首先,於矽基板上成膜由鋁、鐵 而成的觸媒膜,對觸媒膜進行熱處理藉此於觸媒膜表面形成觸媒粒子。接著,在加熱環境中使烴氣體與觸媒粒子接觸,由觸媒粒子開始成長為CNT6,藉此可製作CNT6。 CNT6 can be produced using, for example, the thermal CVD method described in JP 2007-126311 A. In this case, first, a film made of aluminum and iron is formed on a silicon substrate The formed catalyst film is heat-treated to form catalyst particles on the surface of the catalyst film. Next, the hydrocarbon gas is brought into contact with the catalyst particles in a heating environment, and the catalyst particles start to grow into CNT6, thereby making CNT6.
以此所製作的CNT6,在基板上面對基板表面的垂直方向上以直線方式配向,具有所謂數百至數千的高縱橫比(aspect ratio)。從基板裁取CNT6使用。所裁取的CNT6中有可能含有觸媒粒子或其斷片等的觸媒殘渣。觸媒殘渣期望能以在惰性氣體中進行高溫退火、酸處理自CNT6中去除。 The CNT6 produced in this way is aligned in a straight line in the vertical direction facing the surface of the substrate on the substrate, and has a so-called high aspect ratio of hundreds to thousands. Cut CNT6 from the substrate for use. The cut CNT6 may contain catalyst residues such as catalyst particles or fragments. It is expected that the catalyst residue can be removed from CNT6 by high-temperature annealing and acid treatment in an inert gas.
並且,亦可藉由弧放電法、雷射蒸發法等其他製作方法獲得CNT6,然而,期望使用盡量不含有CNT6以外的雜質(觸媒殘渣等)的方法製作CNT6。關於此等雜質,亦期望與觸媒殘渣同樣地去除。 In addition, CNT6 can also be obtained by other production methods such as arc discharge method and laser evaporation method. However, it is desirable to produce CNT6 using a method that does not contain impurities (catalyst residue, etc.) other than CNT6 as much as possible. Regarding these impurities, it is desirable to remove them in the same manner as the catalyst residue.
(3-2)使用製作的CNT而生成CNT分散液的步驟 (3-2) Steps to generate CNT dispersion using the produced CNT
首先,依上述方法所製作的CNT6在預定溫度的氧環境中予以氧化。此時,於CNT6表面的一部份,使羥基或羧基等官能基形成於CNT6表面。可使用臭氧處理器將CNT6氧化,亦可例如將CNT6浸漬於含有1:1比例的硝酸與硫酸的混合酸中使其氧化。 First, the CNT6 produced by the above method is oxidized in an oxygen environment at a predetermined temperature. At this time, on a part of the surface of CNT6, functional groups such as hydroxyl or carboxyl groups are formed on the surface of CNT6. An ozone processor can be used to oxidize CNT6, or, for example, CNT6 can be immersed in a mixed acid containing a 1:1 ratio of nitric acid and sulfuric acid to be oxidized.
接著,將表面經氧化的CNT6以成為預定的質量濃度的方式投入分散溶媒中,利用均質機或高壓剪切、超音波分散機等,使CNT6均勻分散,藉此可生成CNT分散液。據此所作成的CNT分散液係以每1條CNT6物理性的分離未纏繞的狀態分散於分散溶媒中,相對於CNT6的數量,2個以上CNT6凝聚的集合物的比例為10%以下。CNT6為凝聚的集合 物的比例係從TEM圖像測定CNT6的條數及集合物的個數而求得。 Next, CNT6 whose surface has been oxidized is thrown into a dispersion solvent so as to have a predetermined mass concentration, and the CNT6 is uniformly dispersed using a homogenizer, high pressure shear, ultrasonic disperser, etc., to thereby produce a CNT dispersion. The resulting CNT dispersion is dispersed in a dispersion solvent in a physically separated and untangled state per CNT6, and the ratio of aggregates of two or more CNT6 aggregates relative to the number of CNT6 is 10% or less. CNT6 is a condensed collection The ratio of objects is determined by measuring the number of CNT6 and the number of aggregates from the TEM image.
作為分散溶媒,可使用水、醇類(乙醇、甲醇、異丙醇等)、有機溶媒(甲苯、丙酮、THF、MEK、己烷、正己烷、乙醚、二甲苯、乙酸甲酯、乙酸乙酯等)。並且,只要不限制骨架2及CNT6的機能,分散液亦可含有分散劑、界面活性劑、接著劑等。
As a dispersion solvent, water, alcohols (ethanol, methanol, isopropanol, etc.), organic solvents (toluene, acetone, THF, MEK, hexane, n-hexane, ether, xylene, methyl acetate, ethyl acetate, etc.) can be used Wait). In addition, as long as the functions of the
(3-3)使用CNT分散液於碳纖維表面形成CNT構造體的步驟 (3-3) Steps of forming CNT structure on the surface of carbon fiber using CNT dispersion
首先,準備好裁切成預定尺寸的碳奈米紙等作為骨架2。並且,本實施形態的情形為所準備的碳紙具有上述連接部4。
First, prepare carbon nano paper cut into a predetermined size as the
接著,在氧環境中,於預定溫度加熱骨架2,使碳纖維3的表面氧化。此時,碳纖維3表面的一部份,形成羥基或羧基等官能基。碳纖維3的表面,可使用臭氧處理器予以氧化,亦可例如將骨架2浸漬於以1:1的比例含有硝酸及硫酸的混合酸中予以氧化。當碳纖維3的表面氧化時,連接部4的表面亦同時被氧化。
Next, in an oxygen environment, the
接著,於依上述所生成的CNT分散液中,浸漬碳纖維3的表面經氧化的骨架2,CNT分散液中施予剪切或超音波等機械能,可於碳纖維3表面形成CNT構造體5。
Next, in the CNT dispersion liquid produced as described above, the
當CNT分散液中施予剪切或超音波等機械能時,於CNT分散液中,CNT6反覆發生分散狀態與凝聚狀態的可逆性反應狀態。此可逆性反應狀態在CNT分散液中浸漬骨架2時亦發生。故,在骨架2的碳纖維3表面亦發生CNT6的分散
狀態與凝聚狀態的可逆性反應狀態,CNT6從分散狀態移往凝聚狀態時,於碳纖維3表面纏繞附著CNT6,於碳纖維3形成CNT構造體5。
When mechanical energy such as shearing or ultrasonic waves is applied to the CNT dispersion, the CNT6 in the CNT dispersion repeatedly undergoes a reversible reaction state between the dispersed state and the aggregated state. This reversible reaction state also occurs when the
當CNT6凝聚時,CNT6透過形成於碳纖維3表面的羥基或羧基結合,經由在碳纖維3與CNT6之間作用的凡得瓦爾力附著於碳纖維3的表面。
When the CNT6 aggregates, the CNT6 is bonded to the surface of the
此時,CNT6同樣地亦附著於連接部4表面,於連接部4亦形成CNT構造體5。
At this time, the
最後,將骨架2自CNT分散液中取出,可獲得CNT6具有彼此直接連接的網絡構造的CNT構造體5形成於碳纖維3表面的電池用電極1。
Finally, the
並且,藉由重複上述(3-3)使用CNT分散液於碳纖維表面形成CNT構造體的步驟,可形成CNT構造體5的厚度變厚的電池用電極1。在此種情形,第2次以後所使用的CNT分散液,每一次追加CNT6至預定量,同時調整CNT6的濃度,施予機械能使CNT6分散。
Furthermore, by repeating the step (3-3) of forming a CNT structure on the surface of a carbon fiber using a CNT dispersion, the
(4)作用及效果 (4) Function and effect
本實施形態的電池用電極1包括:經疊合複數個碳纖維3而形成3維網狀構造的骨架2;形成於複數個碳纖維3表面的CNT構造體5的構成。再者,CNT構造體5係複數個CNT6形成彼此直接連接的網絡構造,且直接固定於碳纖維3表面的構成。
The
此種電池用電極1,與習知不同,由於不使用接著劑將CNT6直接固定於碳纖維3,構成3維網狀的骨架2無須
透過接著劑黏聚,故不會阻礙電解液的流通,當應用於電池時,可更提升電池的輸出。
This kind of
此外,電池用電極1由於包括形成於碳纖維3表面的CNT構造體5,故可增加比表面積,且CNT6未透過絕緣體而是直接固定於碳纖維3,因此,相較於以往,可抑制電池用電極1電阻的增加,故當應用於電池時,可更提升電池的輸出。
In addition, since the
本實施形態的生化燃料電池使用本實施形態的電池用電極1而構成。
The biochemical fuel cell of this embodiment is constructed using the
此種生化燃料電池,由於電解液或酵素的流通未受到阻礙,因此,較以往更有效率地生成電能,此外,電池用電極1的比表面積大,因此,較以往增加電流密度,可提升電池的輸出。
Since this type of biochemical fuel cell is not obstructed in the flow of electrolyte or enzymes, it generates electric energy more efficiently than in the past. In addition, the
(5)實施例 (5) Example
依上述「(3)本實施形態的電池用電極的製造方法」所示的順序,製作實施例1的電池用電極1。實施例1中,使用依上述熱CVD法於矽基板上成長直徑10~15nm、長度100μm以上的多層碳奈米管作為CNT6。
The
此外實施例1,將所製作的CNT6浸漬於含有3:1比例的硝酸與硫酸的混合酸中,於洗淨後過濾乾燥,藉以去除觸媒殘渣。並且,實施例1為了去除觸媒殘渣而將CNT6浸漬於混合酸中時,CNT6的表面亦受到氧化,故,無須額外施行CNT6的氧化步驟。 In addition, in Example 1, the produced CNT6 was immersed in a mixed acid containing a 3:1 ratio of nitric acid and sulfuric acid, washed and filtered and dried to remove catalyst residue. In addition, in Example 1, when the CNT6 was immersed in a mixed acid in order to remove the catalyst residue, the surface of the CNT6 was also oxidized, so there was no need to perform an additional oxidation step of the CNT6.
再者,實施例1,由於所製作的CNT6的長度為 100μm以上,故,在將CNT6投入至作為分散溶媒的丁酮中後,以超音波均質機將CNT6粉碎成CNT6為0.5~10μm的長度,同時使CNT6均勻分散。在CNT分散液中CNT6的濃度成為0.01wt%。 Furthermore, in Example 1, the length of the produced CNT6 is Therefore, after putting CNT6 into methyl ethyl ketone as a dispersion solvent, CNT6 is pulverized into a length of 0.5-10 μm for CNT6 with an ultrasonic homogenizer, and CNT6 is uniformly dispersed. The concentration of CNT6 in the CNT dispersion is 0.01 wt%.
又,實施例1中,使用Toray股份有限公司製碳紙(型號:TGP-H-120),裁切成100×100mm的尺寸作為骨架2,在密閉容器內(容積1000cc中包含1cc的氧)在500℃加熱骨架2達10分鐘。
Also, in Example 1, carbon paper made by Toray Co., Ltd. (model: TGP-H-120) was used, cut into a size of 100×100 mm as the
對於浸漬該骨架2的CNT分散液,施行28kHz及40kHz的超音波10秒鐘,使碳纖維3表面附著CNT6,藉以製作電池用電極1。之後,從CNT分散液將骨架2取出,在80℃的熱板上乾燥,獲得相對於骨架2,含有約0.1wt%比例CNT6的實施例1的電池用電極1。
The CNT dispersion in which the
實施例1的電池用電極1的表面,以掃瞄式電子顯微鏡(Scanning Electron Microscope:SEM)觀察。如第2圖所示,可確認骨架2具有彼此交纏的複數個碳纖維3接觸的部份、相鄰碳纖維3彼此接觸的部份、以及由複數個碳纖維3形成的網目一部份的連接部4。該連接部4具有CNT構造體5形成於碳纖維3表面之前的骨架2。除了連接部4外,電池用電極1的骨架2中未觀察到黏聚。因此,確認電池用電極1中,形成骨架2的碳纖維3的表面形成CNT構造體5,但骨架2中未產生黏聚。
The surface of the
此外,如第3A圖所示,可確認於碳纖維3的表面形成有由複數個CNT6彼此直接連接的網絡構造所形成的CNT
構造體5。
In addition, as shown in Figure 3A, it can be confirmed that CNTs formed by a network structure in which a plurality of
再者,如第3B圖所示,CNT6可直接固定於碳纖維3表面。
Furthermore, as shown in Figure 3B, CNT6 can be directly fixed on the surface of
使用白金作為輔助電極(counter electrode),Ag-AgCl電極作為參考電極,實施例1的電池用電極1作為試驗電極,PH7的磷酸緩衝液(0.1mol/L)作為電解液,BOD作為酵素,於電解液中將氧還原,測定氧還原電流。此外,作為比較例1,試驗電極替換成在碳紙以PTFE黏著科琴黑製作成習知的電極,在同樣的條件測定氧還原電流。結果,確認使用實施例1的電池用電極1作為試驗電極,相較於使用習知的電極,氧還原電流提升。
Use platinum as the counter electrode, Ag-AgCl electrode as the reference electrode,
(6)變化例 (6) Variations
並且,本發明不限於上述實施形態,在本發明要旨的範圍內可有各種的變化實施。 In addition, the present invention is not limited to the above-mentioned embodiment, and various modifications can be implemented within the scope of the gist of the present invention.
雖然上述實施形態說明電子傳遞介質及氧化還原酵素存在於電解液中的情形,然而,本發明不限於此,電子傳遞介質及氧化還原酵素固定於電池用電極1亦可。
Although the foregoing embodiment described the case where the electron transfer medium and the redox enzyme are present in the electrolyte, the present invention is not limited to this, and the electron transfer medium and the redox enzyme may be fixed to the
雖然上述實施形態說明生化燃料電池的陽極電極與陰極電極兩者使用本發明的電池用電極1的情形,然而,本發明不限於此,僅陽極電極或陰極電極任一者使用電池用電極1亦可。
Although the above embodiment describes the case where the
雖然上述實施形態說明使用本發明的電池用電極1作為生化燃料電池的電極的情形,本發明不限於此,可作為燃料電池、鋰離子二次電池等電池的電極使用。
Although the foregoing embodiment describes the case where the
此外,雖然上述實施形態說明複數個CNT6直接固定於碳纖維3表面的情形,然而,本發明不限於此,複數個CNT6,在碳纖維3表面,可由CNT6表面的一部份作為附著分直接固定,抑或在附著部份以外的至少一部份經由設置接著構件而物理性的固定亦可。
In addition, although the above embodiments describe the case where a plurality of CNT6 are directly fixed on the surface of the
此時,變化例的電池用電極,鄰接著CNT6的附著部份復設置接著構件。接著構件為由熱硬化性樹脂的硬化物所形成者,例如可使用環氧樹脂或樹脂乳化系的黏接劑等。接著構件藉由潤濕接著將CNT6物理性固定於碳纖維3。
At this time, in the battery electrode of the modified example, an adhesive member is provided adjacent to the attachment portion of CNT6. The next member is formed of a cured product of thermosetting resin, and for example, an epoxy resin or a resin emulsified adhesive can be used. Then, the member physically fixes the CNT6 to the
藉此,變化例的電池用電極,由於CNT6在附著部份的周圍,CNT6附著部份以外的至少一部份補強有接著構件,因此,可藉由碳纖維3堅固地固定,在應用於電池中時,可抑制伴隨著CNT6的剝離所造成的電池輸出的降低或電極間的短路,可提升電池的耐久性。
As a result, the battery electrode of the modified example has CNT6 around the attached part, and at least a part of the CNT6 attached part is reinforced with an adhesive member. Therefore, it can be firmly fixed by the
此種變化例的電池用電極,由於CNT6並未與碳纖維3共同覆蓋接著構件而固定於碳纖維3的表面,亦並未隔著接著構件固定於碳纖維3,可抑制因設置接著構件所造成的電極面積的降低及CNT6與碳纖維3之間電阻的增加,應用於電池中時,可提升電池的輸出與耐久性。
The battery electrode of this modified example is fixed to the surface of the
1‧‧‧電池用電極 1‧‧‧Electrode for battery
2‧‧‧骨架 2‧‧‧Frame
3‧‧‧碳纖維 3‧‧‧Carbon Fiber
4‧‧‧連接部 4‧‧‧Connecting part
5‧‧‧碳奈米管構造體 5‧‧‧Carbon Nanotube Structure
6‧‧‧碳奈米管 6‧‧‧Carbon Nanotube
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JP2015073827A JP2016195009A (en) | 2015-03-31 | 2015-03-31 | Electrode for battery and biofuel battery |
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US20130230744A1 (en) * | 2010-11-18 | 2013-09-05 | Japan Science And Technology Agency | Electrode for microbial fuel cell and microbial fuel cell using the same |
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US20130230744A1 (en) * | 2010-11-18 | 2013-09-05 | Japan Science And Technology Agency | Electrode for microbial fuel cell and microbial fuel cell using the same |
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