TW201917750A - Hybrid capacitor - Google Patents
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- TW201917750A TW201917750A TW107124855A TW107124855A TW201917750A TW 201917750 A TW201917750 A TW 201917750A TW 107124855 A TW107124855 A TW 107124855A TW 107124855 A TW107124855 A TW 107124855A TW 201917750 A TW201917750 A TW 201917750A
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/04—Hybrid capacitors
- H01G11/06—Hybrid capacitors with one of the electrodes allowing ions to be reversibly doped thereinto, e.g. lithium ion capacitors [LIC]
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/26—Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features
- H01G11/28—Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features arranged or disposed on a current collector; Layers or phases between electrodes and current collectors, e.g. adhesives
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/30—Electrodes characterised by their material
- H01G11/32—Carbon-based
- H01G11/42—Powders or particles, e.g. composition thereof
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/66—Current collectors
- H01G11/68—Current collectors characterised by their material
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/66—Current collectors
- H01G11/70—Current collectors characterised by their structure
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- 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
- Y02E60/13—Energy storage using capacitors
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Abstract
Description
本發明係關於一種混合式電容器。 The invention relates to a hybrid capacitor.
本申請要求基於2017年7月18日在日本提交的日本專利申請第2017-139523號的優先權,其內容通過引用結合於此。 This application claims priority based on Japanese Patent Application No. 2017-139523 filed in Japan on July 18, 2017, the contents of which are incorporated herein by reference.
以往,作為儲存電能的技術,已知有電雙層電容器(例如,參照專利文獻1)或二次電池。電雙層電容器(EDLC:Electric double layer capacitor)的壽命、安全性、輸出密度皆遠較二次電池優異。然而,電雙層電容器與二次電池相比能量密度(體積能量密度)較低是其課題。 Conventionally, as a technology for storing electric energy, an electric double-layer capacitor (for example, refer to Patent Document 1) or a secondary battery is known. Electric double layer capacitors (EDLCs) have far better life, safety and output density than secondary batteries. However, the electric double-layer capacitor has a lower energy density (volume energy density) than the secondary battery, which is a problem.
此處,電雙層電容器所蓄積的能量(E),係使用電容器的靜電容量(C)與施加電壓(V)以E=1/2×C×V2表示,能量係與靜電容量及施加電壓的平方成正比。因此,為了改善電雙層電容器的能量密度,而提出了提升電雙層電容器之靜電容量或施加電壓的技術。 Here, the energy (E) stored in the electric double-layer capacitor is represented by the capacitance (C) and the applied voltage (V) of the capacitor as E = 1/2 × C × V 2 . The square of the voltage is proportional. Therefore, in order to improve the energy density of the electric double-layer capacitor, a technique for increasing the electrostatic capacity or the applied voltage of the electric double-layer capacitor is proposed.
作為提升電雙層電容器之靜電容量的技術,已知有增大構成電雙層電容器之電極之活性碳的比表面積之技術。現今,已知的活性碳,比表面積為1000m2/g至2500m2/g。於電極使用如此之活性碳的電雙層電容器,係使用將四級銨鹽溶解於有機溶劑的有機電解液、或硫酸等水溶液電解液等作為電解液。 As a technique for increasing the electrostatic capacity of an electric double-layer capacitor, a technique of increasing the specific surface area of activated carbon constituting an electrode of the electric double-layer capacitor is known. Today, known activated carbon has a specific surface area of 1000 m 2 / g to 2500 m 2 / g. An electric double-layer capacitor using such activated carbon as an electrode uses an organic electrolytic solution in which a quaternary ammonium salt is dissolved in an organic solvent, or an aqueous electrolytic solution such as sulfuric acid as the electrolytic solution.
由於有機電解液可使用的電壓範圍廣,可提高施加電壓,故可提升能量密度。 Since the organic electrolyte can be used in a wide range of voltages, the applied voltage can be increased, so the energy density can be increased.
作為利用電雙層電容器之原理來提升電雙層電容器 之施加電壓的技術者,已知有鋰離子電容器。於負極使用可將鋰離子嵌入、脫出的石墨或碳,於正極使用與可吸脫附電解質離子之電雙層電容器之電極材料同等的活性碳者,稱為鋰離子電容器。又,於正極或負極之任一者使用與電雙層電容器之電極材料同等的活性碳,於另一電極使用金屬氧化物、導電性高分子作為產生法拉第反應的電極者,稱為混合式電容器(Hybrid capacitor)。關於鋰離子電容器,構成電雙層電容器之電極中之負極係由鋰離子二次電池之負極材料之石墨或碳黑等所構成,且其石墨或碳黑內嵌入有鋰離子。鋰離子電容器之特徵為,較一般的電雙層電容器、亦即兩極皆由活性碳所構成者,有較大的施加電壓。 Lithium-ion capacitors are known as a technique that uses the principle of an electric double-layer capacitor to increase the voltage applied to the electric double-layer capacitor. The use of graphite or carbon that can insert and desorb lithium ions in the negative electrode and the use of activated carbon equivalent to the electrode material of an electric double-layer capacitor that can absorb and desorb electrolyte ions is called a lithium ion capacitor. In addition, the use of activated carbon equivalent to the electrode material of an electric double-layer capacitor for either the positive electrode or the negative electrode, and the use of a metal oxide or a conductive polymer as the electrode for the Faraday reaction at the other electrode are called hybrid capacitors. (Hybrid capacitor). Regarding lithium ion capacitors, the negative electrode in the electrodes constituting the electric double-layer capacitor is composed of graphite or carbon black, etc. as the negative electrode material of the lithium ion secondary battery, and lithium ions are embedded in the graphite or carbon black. Lithium-ion capacitors are characterized by a larger applied voltage than ordinary electric double-layer capacitors, that is, those whose poles are made of activated carbon.
然而,當於電極使用石墨時,無法使用碳酸丙烯酯作為電解液是其課題。當於電極使用石墨時,碳酸丙烯酯會電解,而於石墨表面附著碳酸丙烯酯的分解生成物,使鋰離子的可逆性降低。碳酸丙烯酯為低溫下亦可動作的溶劑。當於電雙層電容器使用碳酸丙烯酯時,該電雙層電容器於-40℃下亦可動作。因此,於鋰離子電容器中,於電極係使用碳酸丙烯酯不易分解的硬碳。然而,硬碳與石墨相比,電極之每單位體積的容量較低,電壓亦比石墨低(成為昂貴的電位)。因此,鋰離子電容器有能量密度變低等之課題。 However, when graphite is used for the electrode, it is impossible to use propylene carbonate as the electrolytic solution. When graphite is used as an electrode, propylene carbonate is electrolyzed, and a decomposition product of propylene carbonate is attached to the graphite surface, thereby reducing the reversibility of lithium ions. Propylene carbonate is a solvent that can operate at low temperatures. When propylene carbonate is used for an electric double-layer capacitor, the electric double-layer capacitor can also operate at -40 ° C. Therefore, in a lithium ion capacitor, hard carbon that is not easily decomposed by propylene carbonate is used for the electrode system. However, compared with graphite, hard carbon has a lower capacity per unit volume and a lower voltage than graphite (which becomes an expensive potential). Therefore, lithium ion capacitors have problems such as a decrease in energy density.
當重視低溫特性時,於負極使用高容量之石墨是困難的鋰離子電容器將難以進一步高能量密度化。此外,於鋰離子電容器中,由於與鋰離子二次電池之負極同樣地於集電體使用銅箔,當進行2V以下的過放電時,銅會溶析出而引起短路,存在放電容量降低的問題。因此,與能夠放電至0V的電雙層電容器相比,鋰離子電容器的使用方法存在受到限制的問題。 When low-temperature characteristics are important, it is difficult to further increase the energy density of lithium ion capacitors in which it is difficult to use high-capacity graphite for the negative electrode. In addition, in lithium-ion capacitors, copper foil is used for the current collector in the same way as the negative electrode of a lithium-ion secondary battery. When an over-discharge of 2 V or less is performed, copper will dissolve out and cause a short circuit, resulting in a problem of reduced discharge capacity . Therefore, compared with an electric double-layer capacitor capable of discharging to 0 V, there is a problem that the method of using the lithium ion capacitor is limited.
就新概念的電容器而言,利用石墨作為正極活性物質代替活性碳,並利用在石墨層之間嵌入脫離電解質離子的反應開發了一種電容器(例如,參照專利文獻2)。於專利文獻2記載著,於正極活性物質使用活性碳之傳統電雙層電容器,若對正極施加 超過2.5V的電壓則電解液會分解而產生氣體,相對於此,於正極活性物質使用石墨的電雙層電容器,即使於3.5V的充電電壓下,亦不會產生電解液的分解,與於正極活性物質使用活性碳之以往的電雙層電容器相比,能以較高電壓動作。關於循環特性或低溫特性、輸出特性也等於或高於傳統電雙層電容器的特性。石墨之比表面積為活性碳之比表面積的數百分之一,其電解液分解作用的不同,即起因於如此巨大之比表面積的不同。 As a capacitor of a new concept, a capacitor has been developed using graphite as a positive electrode active material instead of activated carbon, and a reaction in which graphite ions are intercalated and detached from electrolyte ions (for example, refer to Patent Document 2). Patent Document 2 describes that a conventional electric double-layer capacitor using activated carbon for a positive electrode active material will decompose the electrolytic solution to generate a gas if a voltage exceeding 2.5 V is applied to the positive electrode. The electric double-layer capacitor does not decompose the electrolyte even at a charging voltage of 3.5V, and can operate at a higher voltage than the conventional electric double-layer capacitor using activated carbon as the positive electrode active material. Regarding the cycle characteristics or low-temperature characteristics, the output characteristics are also equal to or higher than those of the conventional electric double-layer capacitor. The specific surface area of graphite is several hundredths of the specific surface area of activated carbon. The difference in the decomposition of the electrolyte is caused by such a large difference in specific surface area.
在使用石墨作為正極活性物質的新概念的電容器中,因為耐久性不足而在實際應用受到阻礙,但已經發現,通過使用覆蓋有非晶碳膜作為集電體的鋁材料的技術(參照專利文獻3),可以將高溫耐久性能提高到實用水平。這種新概念的電容器是使用在正電極上的石墨層之間嵌入脫離電解質離子的反應的電容器,並且嚴格來說這不是電雙層電容器,但是在專利文獻3中,它在廣義的意義上被稱為電雙層電容器。 In a capacitor of a new concept using graphite as a positive electrode active material, practical applications are hindered due to insufficient durability, but it has been found that by using an aluminum material covered with an amorphous carbon film as a current collector technology (see Patent Literature) 3), can improve the high temperature durability to a practical level. This new concept capacitor is a capacitor that uses a reaction in which the electrolyte ions are intercalated between the graphite layers on the positive electrode, and this is not strictly an electric double layer capacitor, but in Patent Document 3, it is in a broad sense It is called an electric double-layer capacitor.
此處,耐久性之試驗一般係以提高溫度之加速試驗(高溫耐久性試驗、充放電循環試驗)來進行。該試驗可依據JIS D 1401:2009所記載之「耐久性(高溫連續額定電壓施加)試驗」的方法進行。若將溫度由室溫升高10℃則劣化速度約變成2倍。高溫耐久性試驗,例如,於60℃之恆溫槽保持(連續充電)於既定電壓(於本發明為3V以上)2000小時,然後回復至室溫進行充放電,測定此時之放電容量的試驗。於該高溫耐久性試驗之後,較佳為相對於初期之放電容量可滿足放電容量維持率為80%以上。 Here, the durability test is generally performed by an accelerated test (high-temperature durability test, charge-discharge cycle test) to increase the temperature. This test can be performed according to the method of "durability (high-temperature continuous rated voltage application) test" described in JIS D 1401: 2009. If the temperature is increased from room temperature by 10 ° C, the deterioration rate will be approximately doubled. For a high-temperature durability test, for example, it is maintained (continuously charged) in a constant temperature bath at 60 ° C. for a predetermined voltage (3V or more in the present invention) for 2000 hours, and then returned to room temperature for charge and discharge, and a test for measuring the discharge capacity at this time. After this high-temperature durability test, it is preferable that the discharge capacity maintenance ratio with respect to the initial discharge capacity is 80% or more.
專利文獻4公開了通過在活性碳中摻雜氮可以增加EDLC的耐電壓。此外,非專利文獻1公開了在活性碳中摻雜氮,以作為去除廢氣中的SO2的催化劑。 Patent Document 4 discloses that the withstand voltage of EDLC can be increased by doping nitrogen in activated carbon. In addition, Non-Patent Document 1 discloses doping nitrogen in activated carbon as a catalyst for removing SO 2 in exhaust gas.
[先前技術文獻] [Prior technical literature]
[專利文獻] [Patent Literature]
專利文獻1:日本特開2011-046584號公報 Patent Document 1: Japanese Patent Application Laid-Open No. 2011-046584
專利文獻2:日本特開2010-040180號公報 Patent Document 2: Japanese Patent Application Laid-Open No. 2010-040180
專利文獻3:國際公開第2017/216960號 Patent Document 3: International Publication No. 2017/216960
專利文獻4:日本特開第2013-026484號 Patent Document 4: Japanese Patent Laid-Open No. 2013-026484
[非專利文獻] [Non-patent literature]
非專利文獻1:Carbon 41 (2003) 1925-1932 Non-Patent Document 1: Carbon 41 (2003) 1925-1932
使用石墨作為正極活性物質和活性炭作為負極活性物職的混合式電容器需要具有更高的能量密度。在這種情況下,由於用於負極活性物質的活性碳的容量小於用於正極活性物質的石墨的容量,因此電池充電和放電時的容量取決於負極容量。為了增加負極容量,降低負極還原電位是有效的,但是當還原電位太低時,具有:由於電解液的分解而產生氣體,或者由於活性炭的表面被電解質分解的產物所覆蓋而使得比表面積減小及伴隨容量降低,或者由於活性碳本身的分解而發生劣化等等的課題。 Hybrid capacitors using graphite as a positive electrode active material and activated carbon as a negative electrode active material need to have a higher energy density. In this case, since the capacity of the activated carbon for the negative electrode active material is smaller than the capacity of the graphite for the positive electrode active material, the capacity at the time of charge and discharge of the battery depends on the capacity of the negative electrode. In order to increase the capacity of the negative electrode, it is effective to reduce the reduction potential of the negative electrode, but when the reduction potential is too low, it has: the generation of gas due to the decomposition of the electrolyte, or the specific surface area is reduced because the surface of the activated carbon is covered by the product of the electrolyte decomposition And problems associated with a decrease in capacity or degradation due to decomposition of activated carbon itself.
鑑於上述情況,本發明的目的是提供一種通過實現高容量化和高電壓化,進而具有高能量密度和高溫耐久性能優異的混合式電容器。 In view of the above circumstances, an object of the present invention is to provide a hybrid capacitor having high energy density and excellent high-temperature durability by realizing high capacity and high voltage.
本發明人在反覆研究解決上述問題,結果在使用石墨作為正極活性物質及使用活性碳作為負極活性物質的混合式電容器中,通過使用摻雜有氮的負極活性物質降低負極的還原電位來實現負極的高容量化與高電壓化。結果,已經發現可以實現混合式電容器的整個電池的高容量化和高電壓化,以增加使電池高能量密度化並改善高溫耐久性能。此時,如果在EDLC中所廣泛使用的蝕刻鋁用作集電器,則蝕刻鋁可能在某一負極還原電位以下腐蝕,並且也證實優選的是使用覆蓋有非晶質碳薄膜的鋁材的組合。 The inventors have repeatedly researched and solved the above problems. As a result, in a hybrid capacitor using graphite as a positive electrode active material and activated carbon as a negative electrode active material, a negative electrode is realized by reducing the reduction potential of the negative electrode by using a negative electrode active material doped with nitrogen. High capacity and high voltage. As a result, it has been found that it is possible to increase the capacity and voltage of the entire battery of the hybrid capacitor to increase the energy density of the battery and improve the high-temperature durability. At this time, if the etched aluminum widely used in EDLC is used as a current collector, the etched aluminum may corrode below a certain negative electrode reduction potential, and it has also been confirmed that it is preferable to use a combination of aluminum material covered with an amorphous carbon film .
為了解決上述課題,本發明提供以下之手段。 In order to solve the above problems, the present invention provides the following means.
(1):本發明的一態樣係涉及一種混合式電容器,係於60℃和3.5V之定電流定電壓連續充電試驗中可維持放電容量維持率80%以上的時間為1000小時以上者,該混合式電容器包含:一正極側集電體及一負極側集電體,皆由鋁材製成,其中該鋁材係由一非晶質碳薄膜披覆,該非晶質碳薄膜的厚度為60奈米以上及300奈米以下;一正極,包含石墨作為正極活性物質;及一負極,包含活性碳作為負極活性物質,且該活性碳包含氮。 (1) One aspect of the present invention relates to a hybrid capacitor that is capable of maintaining a discharge capacity retention rate of 80% or more for 1000 hours or more in a constant-charge constant-voltage and constant-voltage test at 60 ° C and 3.5V. The hybrid capacitor includes: a positive-side current collector and a negative-side current collector, both of which are made of aluminum material, wherein the aluminum material is covered by an amorphous carbon film, and the thickness of the amorphous carbon film is Above 60 nm and below 300 nm; a positive electrode including graphite as a positive electrode active material; and a negative electrode including activated carbon as a negative electrode active material, and the active carbon includes nitrogen.
(2):在根據上述態樣點的混合式電容器中,可將一氮摻雜處理施加於該活性炭。 (2): In the hybrid capacitor according to the above aspect, a nitrogen doping treatment may be applied to the activated carbon.
(3):在根據上述態樣的混合式電容器中,該活性碳中的氮與碳的比率為1.0at%以上及4.0at%以下。 (3): In the hybrid capacitor according to the aspect described above, the ratio of nitrogen to carbon in the activated carbon is 1.0 at% or more and 4.0 at% or less.
根據本發明可以提供高能量密度化和優異的高溫耐久性能的混合式電容器。 According to the present invention, a hybrid capacitor having high energy density and excellent high-temperature durability can be provided.
第1圖:表示在實施例2中製作的混合式電容器的放電特性(當改變氮摻雜處理時間時,在60℃下進行定電流定電壓連續充電試驗時的放電容量改善率)的圖表。 FIG. 1 is a graph showing the discharge characteristics (discharge capacity improvement rate when a constant-current constant-voltage continuous charge test is performed at 60 ° C. when the nitrogen doping treatment time is changed) of the hybrid capacitor fabricated in Example 2.
第2圖:表示在實施例4中製作的混合式電容器的放電特性(在高電壓區域中充電電壓變化時,在60℃下進行的定電流定電壓連續充電試驗時的放電容量改善率)的圖表。 Fig. 2 shows the discharge characteristics (discharge capacity improvement rate during a constant-current constant-voltage continuous charging test at 60 ° C when the charging voltage changes in a high-voltage region when the charging voltage changes in a high-voltage region) chart.
以下,針對適用本發明之混合式電容器,使用圖式說明其構成。在以下描述中使用的附圖中,為了易於理解特徵,存在為了方便而放大示出特徵部分的情況,並且每個部件的尺寸比率不總是與實際的相同。另外,以下描述中舉例說明的材料、尺寸等僅是示例,並且本發明不限於此,並且可以通過在發揮效果的範圍內適當地改變來實施。 Hereinafter, the structure of a hybrid capacitor to which the present invention is applied will be described using drawings. In the drawings used in the following description, in order to easily understand the features, there are cases where the feature portions are enlarged for convenience, and the size ratio of each component is not always the same as the actual one. In addition, the materials, dimensions, and the like exemplified in the following description are merely examples, and the present invention is not limited thereto, and can be implemented by appropriately changing within a range in which effects are exhibited.
本發明之一實施形態之混合式電容器,於60℃、3.5V之定電流定電壓連續充電試驗中,係可維持放電容量維持率80%以上的時間為1000小時以上之混合式電容器,其特徵為:具備正極、負極、電解液及隔板。一正極側集電體及一負極側集電體皆由鋁材製成,該鋁材由非晶質碳薄膜被覆,該非晶質碳薄膜的厚度為60nm以上、300nm以下。正極含有石墨作為正極活性物質,負極使用活性碳作為負極活性物質,一氮摻雜處理施加於活性碳,活性碳表面的官能團被氮取代,活性碳包含氮。 A hybrid capacitor according to an embodiment of the present invention is a hybrid capacitor capable of maintaining a discharge capacity retention rate of 80% or more for 1,000 hours or more in a constant-current and constant-voltage constant-charge test at 60 ° C and 3.5V. It is equipped with a positive electrode, a negative electrode, an electrolytic solution and a separator. A positive electrode side current collector and a negative electrode side current collector are made of aluminum material, the aluminum material is covered with an amorphous carbon thin film, and the thickness of the amorphous carbon thin film is 60 nm or more and 300 nm or less. The positive electrode contains graphite as a positive electrode active material, the negative electrode uses activated carbon as a negative electrode active material, a nitrogen doping treatment is applied to the activated carbon, the functional groups on the surface of the activated carbon are replaced by nitrogen, and the activated carbon contains nitrogen.
正極,係於集電體(正極側之集電體)上形成正極活性物質層而成。 The positive electrode is formed by forming a positive electrode active material layer on a current collector (a current collector on the positive electrode side).
正極活性物質層,可將含有黏結劑及視需要之量之導電材的漿狀正極材料,塗布於正極側集電體上使其乾燥而形成。 The positive electrode active material layer can be formed by applying a paste-like positive electrode material containing a binder and a conductive material in an amount as needed to the positive electrode current collector and drying it.
黏結劑,例如,可使用聚偏二氟乙烯(PVDF)、聚四氟乙烯(PTFE)、氟橡膠、乙烯丙二烯橡膠、苯乙烯丁二烯、丙烯酸系、烯烴系、羧基甲基纖維素(CMC)系之單獨、或兩種以上的混合系。 Binders, for example, polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE), fluororubber, ethylene-propylene-diene rubber, styrene-butadiene, acrylic, olefin-based, carboxymethyl cellulose can be used (CMC) is a single or a mixture of two or more.
導電材,只要可使正極活性物質的導電性為良好者即可,並無特別限定,可使用周知的導電材。例如,可使用碳黑、碳纖維(包含碳奈米管(CNT)、VGCF(註冊商標)等,不限於碳奈米管)等。 The conductive material is not particularly limited as long as the conductivity of the positive electrode active material is good, and a known conductive material can be used. For example, carbon black, carbon fiber (including carbon nanotube (CNT), VGCF (registered trademark), etc., and not limited to carbon nanotube) can be used.
正電極集電器可以是提高耐腐蝕性的鋁材,例如塗有非晶質碳薄膜的鋁材。鋁材可以僅用非晶質碳薄膜披覆,或者可以在非晶質碳薄膜和正極活性物質之間設置導電碳層。 The positive electrode current collector may be an aluminum material with improved corrosion resistance, such as an aluminum material coated with an amorphous carbon thin film. The aluminum material may be covered only with an amorphous carbon film, or a conductive carbon layer may be provided between the amorphous carbon film and the positive electrode active material.
基材之鋁材,可使用一般集電體用途所使用之鋁材。鋁材之形狀,可做成箔、薄片、薄膜、網等型態。集電體較佳可使用鋁箔。又,該鋁材除平面者之外,亦可使用後述之蝕刻鋁。 As the base material, the aluminum material used for general current collector applications can be used. The shape of aluminum can be made into foil, sheet, film, net, etc. As the current collector, aluminum foil is preferably used. In addition to this aluminum material, etched aluminum described later can be used in addition to flat ones.
當鋁材為箔、薄片、薄膜時,其厚度並無特別限定,但當電池本身的尺寸相同時,有愈薄則能封入電池盒之活性物質 愈多的優點,但由於存在強度降低的缺點,需選擇適當的厚度,。實際厚度以10μm至40μm為佳、更佳為15μm至30μm。當厚度未滿10μm時,於使鋁材表面粗面化的步驟、或於其他製造步驟中,鋁材有破裂或產生龜裂之虞。 When the aluminum material is foil, sheet, or film, its thickness is not particularly limited, but when the battery itself has the same size, the thinner the more active material that can be enclosed in the battery case, but the disadvantage of reduced strength , Need to choose the appropriate thickness. The actual thickness is preferably 10 μm to 40 μm , and more preferably 15 μm to 30 μm . When the thickness is less than 10 μm , the aluminum material may be cracked or cracked in the step of roughening the surface of the aluminum material or in other manufacturing steps.
以非晶質碳薄膜被覆的鋁材,亦可使用蝕刻鋁。 An aluminum material coated with an amorphous carbon film may also be etched aluminum.
蝕刻鋁係藉由蝕刻進行粗面化處理者。蝕刻一般可使用浸漬於鹽酸等酸溶液(化學蝕刻)、或於鹽酸等酸溶液中以鋁作為陽極進行電解(電化學蝕刻)之方法等。於電化學蝕刻,由於電解時之電流波形、溶液之組成、溫度等會使蝕刻形狀不同,故可由電容器性能的觀點加以選擇。 Etching aluminum is a roughening process by etching. Generally, etching can be performed by immersing in an acid solution such as hydrochloric acid (chemical etching), or electrolytically (electrochemical etching) using aluminum as an anode in an acid solution such as hydrochloric acid. In electrochemical etching, the shape of the etching is different because of the current waveform, the composition of the solution, and the temperature during electrolysis, so it can be selected from the viewpoint of capacitor performance.
鋁材可使用於表面具備鈍化層或不具備鈍化層之任一者。鋁材於其表面形成有自然氧化膜之鈍化膜的時候,非晶質碳鈍化層可設置於該自然氧化膜之上,或者,例如也可將自然氧化層以氬濺鍍除去後再設置。 The aluminum material can be used on either a surface with or without a passivation layer. When a passivation film of a natural oxide film is formed on the aluminum material, an amorphous carbon passivation layer may be disposed on the natural oxide film, or, for example, the natural oxide layer may be removed by argon sputtering and then provided.
鋁材上之自然氧化膜為鈍化膜,其本身有不易被電解液侵蝕的優點,另一方面,亦與集電體電阻的增大相關,故由減低集電體電阻的觀點,以無自然氧化膜為佳。 The natural oxide film on aluminum is a passive film, which has the advantage of not being easily eroded by the electrolyte. On the other hand, it is also related to the increase of the collector resistance. Therefore, from the viewpoint of reducing the collector resistance, An oxide film is preferred.
本說明書中,所謂非晶質碳薄膜,係非晶質之碳膜或氫化碳膜,包含類鑽碳(DLC)膜、碳硬質膜、非晶質碳(a-C)膜、氫化非晶質碳(a-C:H)膜等。非晶質碳薄膜之成膜方法,可使用採用烴系氣體之電漿CVD法、濺鍍蒸鍍法、離子鍍著法、真空電弧蒸鍍法等周知之方法。又,非晶質碳薄膜較佳為具有作為集電體之功能程度的導電性。 In this specification, an amorphous carbon thin film refers to an amorphous carbon film or a hydrogenated carbon film, and includes a diamond-like carbon (DLC) film, a carbon hard film, an amorphous carbon (aC) film, and a hydrogenated amorphous carbon. (aC: H) film and the like. As a method for forming the amorphous carbon thin film, a known method such as a plasma CVD method using a hydrocarbon-based gas, a sputtering evaporation method, an ion plating method, and a vacuum arc evaporation method can be used. In addition, the amorphous carbon thin film preferably has a degree of conductivity that functions as a current collector.
例示之非晶質碳薄膜的材料之中,類鑽碳係具有混合存在鑽石鍵(SP3)與石墨鍵(SP2)兩者之非晶質結構的材料,具有高耐藥品性。然而,當使用於集電體之薄膜時導電性低,故為了提高導電性,較佳為摻雜硼或氮。 Among the exemplified materials of the amorphous carbon thin film, the diamond-like carbon is a material having an amorphous structure in which both a diamond bond (SP 3 ) and a graphite bond (SP 2 ) are mixed, and has high chemical resistance. However, when a thin film is used for a current collector, the conductivity is low, so in order to improve the conductivity, it is preferable to dope boron or nitrogen.
非晶質碳薄膜的厚度較佳為60nm以上及300nm以下。非晶質碳薄膜的膜厚,若未滿60nm則過薄使得非晶質碳薄膜 的被覆效果變小,無法充分抑制定電流定電壓連續充電試驗中集電體的腐蝕,若超過300nm變得過厚則非晶質碳薄膜變成電阻體,而與活性物質層之間的電阻升高。因此,較佳的是適當選擇適合的厚度。非晶質碳薄膜的厚度,較佳為80nm以上、300nm以下,更佳為120nm以上、300nm以下。當藉由使用烴系氣體之電漿CVD法形成非晶質碳薄膜時,非晶質碳薄膜的厚度可藉注入於鋁材的能量,具體而言可由施加電壓、施加時間、溫度進行控制。 The thickness of the amorphous carbon thin film is preferably 60 nm or more and 300 nm or less. If the thickness of the amorphous carbon thin film is less than 60 nm, the thickness of the amorphous carbon thin film is too small, and the corrosion of the current collector in the constant current and constant voltage continuous charging test cannot be sufficiently suppressed. If it is too thick, the amorphous carbon thin film becomes a resistor, and the resistance to the active material layer increases. Therefore, it is preferable to appropriately select a suitable thickness. The thickness of the amorphous carbon thin film is preferably 80 nm or more and 300 nm or less, and more preferably 120 nm or more and 300 nm or less. When an amorphous carbon thin film is formed by a plasma CVD method using a hydrocarbon-based gas, the thickness of the amorphous carbon thin film can be controlled by the energy injected into the aluminum material, specifically, by applying a voltage, a time, and a temperature.
本實施例之混合式電容器所使用之正極活性物質,係含有石墨者。石墨,可使用人造石墨、天然石墨之任一者。又,天然石墨已知有鱗片狀與土狀。天然石墨,是藉由將所挖掘之原礦石粉碎、反覆進行稱為懸浮選礦法之選礦而得。又,人造石墨,例如係經藉由高溫將碳材料進行燒製的石墨化步驟所製造者。更具體而言,例如,可於原料焦碳添加瀝青等結合劑以成形,藉由加熱至1300℃左右進行一次燒製,接著使一次燒製品含浸於瀝青樹脂,再以接近3000℃的高溫進行二次燒製而製得。另外,也可以使用石墨顆粒表面塗有碳的塗層。 The positive electrode active material used in the hybrid capacitor of this embodiment is one containing graphite. As the graphite, any of artificial graphite and natural graphite can be used. In addition, natural graphite is known to be scaly and earthy. Natural graphite is obtained by pulverizing the excavated raw ore and repeatedly performing a beneficiation method called a suspension beneficiation method. The artificial graphite is produced, for example, by a graphitization step of firing a carbon material at a high temperature. More specifically, for example, a binder such as pitch can be added to the raw coke for molding, and the firing can be performed by heating to about 1300 ° C, then impregnating the primary fired product with the asphalt resin, and then performing the high temperature approaching 3000 ° C. It is obtained by secondary firing. Alternatively, a coating having carbon on the surface of the graphite particles may be used.
又,石墨的結晶構造,大致可分為由ABAB所構成之層構造的六方晶、與由ABCABC所構成之層構造的菱面體晶。該等係視條件成為該等構造之單獨、或混合狀態,但任一結晶構造者或混合狀態者皆可使用。例如,後述之實施例所使用之益瑞石石墨和碳日本(‧‧)股份公司製KS-6(商品名)之石墨的菱面體晶的比率為26%,大阪氣體化學股份有限公司製之人造石墨的介穩相球狀碳(MCMB),菱面體晶的比率為0%。 The crystal structure of graphite can be roughly divided into a hexagonal crystal having a layer structure composed of ABAB and a rhombohedral crystal having a layer structure composed of ABCABC. Depending on the conditions, these structures are singular or mixed, but any crystal structure or mixed state can be used. For example, the erythrite graphite and carbon Japan used in the examples described later ( ‧ ‧ ) The ratio of rhombohedral crystals of graphite made by KS-6 (trade name) of the joint-stock company is 26%. The ratio is 0%.
於本實施例中使用的石墨,與以往之EDLC所使用的活性碳相比,其靜電容量的展現機制不同。在活性碳的情況下,利用大的比表面積,電解質離子在其表面上吸脫附以產生靜電容量。相對於此,在石墨的情況下,通過為電解質離子的陰離子在石墨層間的嵌入脫離(嵌入-脫出;Intercalation-Deintercalation)來 展現靜電容量。由於這種差異,在專利文獻3中將根據本實施例的使用石墨的混合電容器在廣義上稱為電雙層電容器,但是與使用具有電雙層的活性碳的EDLC不同。 The graphite used in this embodiment has a different mechanism for displaying electrostatic capacity than the activated carbon used in the conventional EDLC. In the case of activated carbon, with a large specific surface area, electrolyte ions are adsorbed and desorbed on its surface to generate an electrostatic capacity. On the other hand, in the case of graphite, the electrostatic capacity is exhibited by intercalation and deintercalation (intercalation-deintercalation) of anions which are electrolyte ions between the graphite layers. Due to this difference, the hybrid capacitor using graphite according to the present embodiment is referred to as an electric double-layer capacitor in the broad sense in Patent Document 3, but is different from an EDLC using activated carbon having an electric double layer.
由於本實施型態使用的集電體在鋁材的表面上具有非晶質碳薄膜,因此防止鋁材與電解液接觸,並且能防止集電體被電解液腐蝕 Since the current collector used in this embodiment has an amorphous carbon film on the surface of the aluminum material, the aluminum material is prevented from contacting the electrolyte, and the current collector can be prevented from being corroded by the electrolyte.
負極係於集電體(負極側集電體)上形成負極活性物質層而成。 The negative electrode is formed by forming a negative electrode active material layer on a current collector (negative electrode side current collector).
負極活性物質層,可將主要含有負極活性物質、黏結劑、及視需要之量之導電材的漿狀負極材料,塗布於負極集電體上使其乾燥而形成。 The negative electrode active material layer can be formed by applying a slurry negative electrode material mainly containing a negative electrode active material, a binder, and a conductive material in an amount as needed, to the negative electrode current collector.
負極活性物質,可使用能將電解質離子之陽離子吸脫附的碳質材料之活性碳。活性碳中所含有氮較佳是通過氮摻雜處理而摻雜於活性碳中。 As the negative electrode active material, activated carbon of a carbonaceous material capable of desorbing and desorbing cations of electrolyte ions can be used. The nitrogen contained in the activated carbon is preferably doped in the activated carbon by a nitrogen doping treatment.
作為負極的集電體,可以與正極側集電體同樣使用耐腐蝕性提高的鋁材,例如,塗覆有非晶質碳薄膜的鋁材。鋁材可以僅覆蓋有非晶質碳薄膜,或者可以在非晶質碳薄膜和負極活性物質之間設置導電碳層。 As the current collector of the negative electrode, an aluminum material having improved corrosion resistance can be used similarly to the current collector on the positive electrode side, for example, an aluminum material coated with an amorphous carbon thin film. The aluminum material may be covered only with an amorphous carbon thin film, or a conductive carbon layer may be provided between the amorphous carbon thin film and the negative electrode active material.
黏結劑,例如,可使用聚偏二氟乙烯(PVDF)、聚四氟乙烯(PTFE)、氟橡膠、乙烯丙二烯橡膠、苯乙烯丁二烯、丙烯酸系、烯烴系、羧基甲基纖維素(CMC)系之單獨、或兩種以上的混合系。 Binders, for example, polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE), fluororubber, ethylene-propylene-diene rubber, styrene-butadiene, acrylic, olefin-based, carboxymethyl cellulose can be used (CMC) is a single or a mixture of two or more.
導電材,只要可使負極活性物質層的導電性為良好者即可,並無特別限定,可使用周知的導電材。例如,可使用碳黑、碳纖維(包含碳奈米管(CNT)、VGCF(註冊商標)等,不限於碳奈米管)等。 The conductive material is not particularly limited as long as the conductivity of the negative electrode active material layer is good, and a known conductive material can be used. For example, carbon black, carbon fiber (including carbon nanotube (CNT), VGCF (registered trademark), etc., and not limited to carbon nanotube) can be used.
對於活性碳的氮摻雜處理,雖可以使用已知的處理,但也可以通過下述方式,例如將負極的表面暴露於氨氣中,或者如在專利文獻4中所公開般的將負極的表面暴露於氨基甲酸 銨並且伴隨進行高溫處理,或者通過將作為氮源的材料添加到在製造活性碳時的原料中來合成。 For the nitrogen-doping treatment of the activated carbon, a known treatment may be used, but it may also be performed by, for example, exposing the surface of the negative electrode to ammonia gas, or exposing the negative electrode to a negative electrode as disclosed in Patent Document 4. The surface is exposed to ammonium carbamate with high temperature treatment, or is synthesized by adding a material as a nitrogen source to a raw material when producing activated carbon.
作為氮摻雜處理裝置,適合的是電爐、或特別是為了能使氨氣對活性碳進行均一性接觸處理的迴轉窯裝置。處理溫度優選在600℃至900℃的範圍內。如果處理溫度過低,則氮摻雜反應難以進行。相反的,如果溫度超過900℃,則活性碳本身的細孔會收縮,活性碳的比表面積會減小而導致容量降低,因此是不佳的。如果處理溫度為900℃或更低,則不會擔心細孔在接近活性碳生產過程的上限溫度時會收縮。 As the nitrogen-doping treatment device, an electric furnace or a rotary kiln device for uniformly contacting activated carbon with activated carbon is suitable. The processing temperature is preferably in the range of 600 ° C to 900 ° C. If the processing temperature is too low, the nitrogen doping reaction is difficult to proceed. Conversely, if the temperature exceeds 900 ° C, the pores of the activated carbon itself will shrink, and the specific surface area of the activated carbon will decrease, resulting in a decrease in capacity, which is not good. If the processing temperature is 900 ° C or lower, there is no concern that the pores will shrink as they approach the upper limit temperature of the activated carbon production process.
在氮摻雜中,待摻雜的氮與碳的比率(N/C比率)根據處理溫度、氣體流速、濃度、處理時間等而變化。N/C比率優選為0.7at%(原子組成百分比)以上,更優選的是1.0at%以上及4.0at%以下,進一步優選的是1.5at%以上及3.0at%以下,特別優選的為2.0at%以上且3.0at%以下。如果氮的摻雜量太小,則降低還原電位的效果降低。而如果太多,則作為活性碳的容量降低,因此在以上述範圍內並與石墨正極進行組合以最佳條件來使用。氮與碳的比率(N/C比率)可通過燃燒法或X射線光電子能譜法(XPS:X-ray photoelectron spectroscopy)測定。 In nitrogen doping, the ratio of nitrogen to carbon (N / C ratio) to be doped varies depending on the processing temperature, gas flow rate, concentration, processing time, and the like. The N / C ratio is preferably 0.7 at% (atomic composition percentage) or more, more preferably 1.0 at% or more and 4.0 at% or less, still more preferably 1.5 at% or more and 3.0 at% or less, and particularly preferably 2.0 at % To 3.0at%. If the doping amount of nitrogen is too small, the effect of reducing the reduction potential is reduced. On the other hand, if it is too much, the capacity as an activated carbon decreases, and therefore, it is used under optimal conditions in the above range in combination with a graphite positive electrode. The ratio of nitrogen to carbon (N / C ratio) can be measured by a combustion method or an X-ray photoelectron spectroscopy (XPS).
在燃燒法中,通過燃燒樣品,樣品中的氮汽化形成NOx氣體後,然後將其還原為N2氣體,另外,碳被汽化成CO氣體或CO2氣體,並且所獲得的N2氣體和CO氣體或CO2氣體分別通過色譜法(檢測器:TCD)定量。X射線光電子能譜是通過用X射線照射樣品的表面並測量從樣品的表面發射的光電子的動能來分析構成樣品表面的元素(N和C)的組成的方法。 In the combustion method, by burning a sample, nitrogen in the sample is vaporized to form NOx gas, and then it is reduced to N 2 gas. In addition, carbon is vaporized to CO gas or CO 2 gas, and the obtained N 2 gas and CO The gas or CO 2 gas was quantified by chromatography (detector: TCD), respectively. X-ray photoelectron spectroscopy is a method of analyzing the composition of elements (N and C) constituting the surface of a sample by irradiating the surface of the sample with X-rays and measuring the kinetic energy of photoelectrons emitted from the surface of the sample.
電解液可採用使用有機溶劑的有機電解液。電解液含有可吸脫附於電極的電解質離子。電解質離子的種類,以離子徑儘可能小者為佳。具體而言,可使用銨鹽或磷鹽、或者離子液體及鋰鹽等。 The electrolytic solution may be an organic electrolytic solution using an organic solvent. The electrolyte contains electrolyte ions that can be desorbed and attached to the electrode. The type of electrolyte ions is preferably as small as possible. Specifically, an ammonium salt or a phosphorus salt, or an ionic liquid, a lithium salt, or the like can be used.
銨鹽能使用四乙銨(TEA)鹽、三乙銨(TEMA)鹽等。 又,磷鹽能使用具有兩個五元環的螺化合物等。 As the ammonium salt, tetraethylammonium (TEA) salt, triethylammonium (TEMA) salt, or the like can be used. As the phosphorus salt, a spiro compound having two five-membered rings can be used.
離子液體的種類並無特別限定,由電解質離子的移動容易程度考量,較佳為黏度儘可能低、或導電性(導電率)高的材料。構成離子液體的陽離子,具體而言,可舉例如咪唑鎓離子、吡啶鎓離子等。咪唑鎓離子可舉例如1-乙基-3-甲基咪唑鎓(1-ethyl-3-methylimidazolium)(EMIm)離子、1-甲基-1-丙基吡咯啉鎓(1-methyl-1-propyl-pyrrolizinium)(MPPy)離子、1-甲基-1-丙基呱嗪鎓(1-methyl-1-propyl-piperizinium)(MPPi)離子等。此外,可以使用四氟硼酸鋰LiBF4,六氟磷酸鋰LiPF6等作為鋰鹽。 The type of the ionic liquid is not particularly limited, and considering the ease of movement of electrolyte ions, a material having as low a viscosity as possible or high conductivity (conductivity) is preferred. Specific examples of the cation constituting the ionic liquid include an imidazolium ion and a pyridinium ion. Examples of the imidazolium ion include 1-ethyl-3-methylimidazolium (EMIm) ion, and 1-methyl-1-propylpyrrolinium (1-methyl-1- propyl-pyrrolizinium (MPPy) ion, 1-methyl-1-propyl-piperizinium (MPPi) ion, and the like. In addition, lithium tetrafluoroborate LiBF 4 , lithium hexafluorophosphate LiPF 6 and the like can be used as the lithium salt.
吡啶鎓離子可舉例如1-乙基吡啶鎓(1-ethylpyridnium)離子、以及1-丁基吡啶鎓(1-buthylpyridnium)離子等。 Examples of the pyridinium ion include a 1-ethylpyridium ion, and a 1-buthylpyridnium ion.
構成離子液體的陰離子可舉例如BF4離子、PF6離子、[(CF3SO2)2N]離子、FSI(雙(氟磺醯基)亞胺;bis(fluorosulfonyl)imide)離子、TFSI(雙(三氟甲磺醯基)亞胺;bis(trifluorosulfonyl)imide)離子等。 Examples of the anion constituting the ionic liquid include BF 4 ion, PF 6 ion, [(CF 3 SO 2 ) 2 N] ion, FSI (bis (fluorosulfonyl) imide; bis (fluorosulfonyl) imide) ion, and TFSI ( Bis (trifluorosulfonyl) imine; bis (trifluorosulfonyl) imide).
溶劑可使用乙腈、碳酸丙烯酯、碳酸二甲酯、碳酸二乙酯、碳酸甲乙酯、二甲基碸、乙基異丙基碸、碳酸乙酯、氟碳酸亞乙酯、γ丁內酯、環丁碸、N,N-二甲基甲醯胺、或二甲亞碸等之單獨或混合溶劑。 As the solvent, acetonitrile, propylene carbonate, dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, dimethylphosphonium, ethylisopropylphosphonium, ethyl carbonate, fluoroethylene carbonate, and gamma butyrolactone can be used. , Cyclobutane, N, N-dimethylformamide, or dimethylmethane, etc., alone or in a mixed solvent.
隔板,由於防止正極及負極短路、或確保電解液保存性等理由,較佳為纖維素系之紙狀隔板、玻璃纖維隔板、或諸如聚乙烯或聚丙烯的微孔膜等。 The separator is preferably a cellulose-based paper separator, a glass fiber separator, or a microporous film such as polyethylene or polypropylene, for reasons such as preventing the positive and negative electrodes from being short-circuited or ensuring the electrolyte storage stability.
如上所述,在根據本實施型態的混合式電容器中,使用含氮的活性碳作為負極活性物質,優選的是通過氮摻雜處理,以使用摻雜有氮的活性碳。當活性碳經受氮摻雜處理時,存在於活性碳表面上的官能團被氮所取代。例如,使用在表面上存在有官能團的活性碳作為負極活性物質時,如果增加在低電位(還原側)的方向上的電極電位(以電池來看的話是指電池電壓增高的 方向),所述官能團與電解質溶液反應而生成有機分解產物或分解氣體。當產生的有機分解產物積聚在活性碳的表面上並且活性碳的表面被有機分解產物覆蓋時,活性碳的比表面積減小並且負極的容量降低。相對於此,當進行氮摻雜時,即使負極的電極電位在低電位(還原側)的方向上增加,由於與電解液反應的官能團被氮取代,因此可以抑制分解氣體或有機分解產物的生成。因此,關於本實施型態的混合式電容器,通過使用以氮摻雜處理使表面上的官能團被氮取代的含氮的活性碳作為負極活性物質,以降低負極的還原電位而實現負極的高容量化和高電壓化,旨在實現使用石墨作為正極活性物質來增加混合式電容器的整個電池的容量和電壓,以實現電池的高能量密度化並改善高溫耐久性能。 As described above, in the hybrid capacitor according to the embodiment, a nitrogen-containing activated carbon is used as a negative electrode active material, and it is preferable to use a nitrogen doping treatment to use a nitrogen-doped activated carbon. When the activated carbon is subjected to a nitrogen doping treatment, the functional groups present on the surface of the activated carbon are replaced with nitrogen. For example, when using an activated carbon having a functional group on the surface as a negative electrode active material, if the electrode potential in the direction of a low potential (reduction side) is increased (in the case of a battery, the direction in which the battery voltage increases), The functional group reacts with the electrolyte solution to generate an organic decomposition product or a decomposition gas. When the generated organic decomposition product accumulates on the surface of the activated carbon and the surface of the activated carbon is covered with the organic decomposition product, the specific surface area of the activated carbon decreases and the capacity of the negative electrode decreases. In contrast, when nitrogen doping is performed, even if the electrode potential of the negative electrode increases in the direction of a low potential (reduction side), since the functional group that reacts with the electrolytic solution is replaced by nitrogen, the generation of a decomposition gas or an organic decomposition product can be suppressed. . Therefore, regarding the hybrid capacitor of the present embodiment, a high capacity of the negative electrode is achieved by using a nitrogen-containing activated carbon in which a functional group on the surface is replaced with nitrogen as a negative electrode active material with a nitrogen doping treatment to reduce the reduction potential of the negative electrode. In order to increase the capacity and voltage of the entire battery of the hybrid capacitor using graphite as a positive electrode active material, the purpose is to increase the capacity and voltage of the battery in order to achieve high energy density of the battery and improve high-temperature durability.
本實施方案中,使用覆蓋有非晶質碳薄膜的鋁箔的使用氮摻雜處理的活性碳的負極不限於在混合式電容器中使用。使用經過氮摻雜處理的活性碳的負極也可以通過使用氮摻雜的活性碳、未摻雜氮的活化碳等用作正極而用作EDLC電極。 In this embodiment, a negative electrode using activated carbon with a nitrogen doping treatment using an aluminum foil covered with an amorphous carbon thin film is not limited to use in a hybrid capacitor. The negative electrode using a nitrogen-doped activated carbon can also be used as an EDLC electrode by using a nitrogen-doped activated carbon, an undoped nitrogen-activated carbon, or the like as a positive electrode.
以下,藉由實施例將使本發明的效果更清楚。應注意,本發明不限於以下實施例,但可以在發揮效果的範圍內通過適當的改變來實施。 In the following, the effects of the present invention will be made clearer by examples. It should be noted that the present invention is not limited to the following embodiments, but may be implemented by appropriate changes within a range in which effects are exhibited.
[實施例1] [Example 1]
秤取由Kureha公司製造的10克活性碳(商品名:YP50F)作為負極活性物質,然後置於由高砂工業公司製造的台式迴轉窯裝置中,以5升/分的流速流通氮氣的同時並將活性碳加熱至800℃。接著,將該氮氣換成氨氣,並在以5升/分的流速流動的同時在800℃下進行熱處理20分鐘。接著,將該氨氣換成氮氣,從裝置中取出冷卻至室溫的活性炭。要提到的是,氮摻雜處理時間是指在升溫之後保持在800℃下(熱處理)的同時並使氨氣流通以在活性碳中摻雜氮的時間。 10 grams of activated carbon (trade name: YP50F) manufactured by Kureha was weighed out as a negative electrode active material, and then placed in a benchtop rotary kiln device manufactured by Takasago Industrial Co., Ltd. while flowing nitrogen at a flow rate of 5 liters / minute while The activated carbon was heated to 800 ° C. Next, this nitrogen gas was replaced with ammonia gas, and a heat treatment was performed at 800 ° C. for 20 minutes while flowing at a flow rate of 5 liters / minute. Next, this ammonia gas was replaced with nitrogen gas, and the activated carbon cooled to room temperature was taken out of the apparatus. It is to be noted that the nitrogen doping treatment time refers to a time in which an ammonia gas flow is allowed to pass through the activated carbon while maintaining the temperature at 800 ° C. (heat treatment) after the temperature rise.
根據燃燒法,取出的活性碳的N/C比率(氮與碳的比 率)計算為2.1at%。要提到的是,被氮摻雜的是活性碳的官能團,官能團僅存在於活性碳表面,但在燃燒法中是以活性碳整體作為對象進行測量的數值計算方法,而不是以活性碳表面為對象。 According to the combustion method, the N / C ratio (ratio of nitrogen to carbon) of the extracted activated carbon was calculated to be 2.1 at%. It should be mentioned that nitrogen is doped with activated carbon functional groups. Functional groups exist only on the surface of activated carbon, but in the combustion method, the numerical calculation method is based on the measurement of the entire activated carbon as opposed to the activated carbon surface. As an object.
將通過上述處理進行氮摻雜處理而以氮置換表面的官能團的含氮的活性碳(下文中有時稱為“氮摻雜的活性碳”)、乙炔黑、聚偏二氟乙烯以80:10:10的重量百分比濃度(wt%)的比率秤量後,以N-甲基吡咯酮溶解混合而得之漿料,使用刮刀塗布於塗有DLC的鋁箔(厚度20μm)上作為負極。 Nitrogen-containing activated carbon (hereinafter sometimes referred to as "nitrogen-doped activated carbon"), acetylene black, and polyvinylidene fluoride were replaced with nitrogen by replacing the functional groups on the surface with nitrogen by nitrogen doping treatment by the above treatment: After weighing at a ratio of 10:10 weight percent concentration (wt%), the slurry obtained by dissolving and mixing with N-methylpyrrolidone was coated on a DLC-coated aluminum foil (thickness: 20 μm) using a doctor blade as a negative electrode.
上述塗有DLC的鋁箔(下文中有時稱為“DLC塗覆鋁箔”)是負極側集電器,並且相當於覆蓋有非晶質碳薄膜的鋁材。DLC被覆鋁箔之製造法,係對純度99.99%之鋁箔,以氬濺鍍將鋁箔表面之自然氧化膜除去後,於該鋁表面附近,於甲烷、乙炔及氮的混合氣體中放電使產生電漿,藉由對鋁材施加負的脈衝電壓使DLC膜生成。此處,對DLC被覆之鋁箔上之DLC膜厚度,以BRUKER公司製探針式表面形狀測定器DektakXT進行計測,結果為135nm。 The above-mentioned DLC-coated aluminum foil (hereinafter sometimes referred to as "DLC-coated aluminum foil") is a negative-electrode-side current collector and corresponds to an aluminum material covered with an amorphous carbon thin film. The manufacturing method of DLC-coated aluminum foil is to remove the natural oxide film on the surface of the aluminum foil by argon sputtering on the aluminum foil with a purity of 99.99%, and then discharge the plasma near the aluminum surface in a mixed gas of methane, acetylene and nitrogen to generate plasma The DLC film is generated by applying a negative pulse voltage to the aluminum material. Here, the thickness of the DLC film on the DLC-coated aluminum foil was measured with a probe type surface shape measuring device DektakXT made by BRUKER, and the result was 135 nm.
將益瑞石石墨和碳日本(‧‧ )股份公司製石墨(商品名:KS-6)、乙炔黑、聚偏二氟乙烯以80:10:10的重量百分比濃度(wt%)的比率秤量,並以N-甲基吡咯酮溶解混合而得作為正極活性物質的漿料,使用刮刀將該漿料塗布於用在與上述負極相同的DLC塗覆鋁箔(厚度20μm)上來製備正極。 Will Iris graphite and carbon Japan ( ‧ ‧ ) Graphite (commercial name: KS-6), acetylene black, and polyvinylidene fluoride manufactured by the joint stock company are weighed at a weight percentage concentration (wt%) of 80:10:10, and dissolved and mixed with N-methylpyrrolidone A positive electrode active material slurry was obtained, and the slurry was applied to a DLC-coated aluminum foil (thickness: 20 μm ), which was the same as the negative electrode, using a doctor blade to prepare a positive electrode.
接著,將上述正極與負極沖孔為直徑16mm的圓盤狀,並以150℃真空乾燥24小時後,移動至氬氣手套工作箱。將該等通過日本高度紙工業股份公司製造的紙隔板進行積層並且添加0.1mL的電解液(其中該電解液使用1M之TEA-BF4(四乙銨四氟硼酸鹽)作為電解質,及SL+DMS(環丁碸(Sulfolane)+二甲基硫醚)作為溶劑),於氬氣手套工作箱中製作2032型鈕扣型電池。 Next, the positive electrode and the negative electrode were punched into a disk shape with a diameter of 16 mm, and vacuum-dried at 150 ° C. for 24 hours, and then moved to an argon glove working box. These were laminated through a paper separator manufactured by Nippon Kogyo Paper Industry Co., Ltd. and 0.1 mL of an electrolytic solution (wherein the electrolytic solution used 1M TEA-BF 4 (tetraethylammonium tetrafluoroborate) as an electrolyte, and SL + DMS (Sulfolane + dimethyl sulfide) as a solvent), and a 2032 type button battery was produced in an argon glove working box.
對於製得之電池,使用Nagano股份公司製的充放電 試驗裝置BTS2004,於20℃之恆溫槽中,以0.4mA/cm2之電流密度在0至3.5V之電壓範圍進行充放電試驗,測量定電流定電壓連續充電試驗前的放電容量。又,施加電壓之上限,於使用氮摻雜活性碳作為負極活性物質之實施例1、實施例2(如後所述)及實施例3(如後所述)可施加至3.5V為止,但於使用沒有進行氮摻雜處理的活性碳作為負極活性物質之比較例1(如後所述)則測定至2.5V為止。 For the obtained battery, a charge-discharge test device BTS2004 made by Nagano Co., Ltd. was used in a constant-temperature bath at 20 ° C to conduct a charge-discharge test at a current density of 0.4 mA / cm 2 in a voltage range of 0 to 3.5 V. Discharge capacity before constant current and constant voltage charging test. In addition, the upper limit of the applied voltage can be applied to 3.5V in Example 1, Example 2 (described later), and Example 3 (described later) using nitrogen-doped activated carbon as a negative electrode active material, but In Comparative Example 1 (which will be described later) using an activated carbon that has not been subjected to a nitrogen doping treatment as a negative electrode active material, it was measured up to 2.5V.
接著,使用充放電試驗裝置,於60℃之恆溫槽中,以充電電流0.4mA/cm2、電壓3.5V進行2000小時之連續充電試驗(定電流定電壓連續充電試驗)。具體而言,在充電期間的預定時間內停止充電,將電池轉移至25℃的恆溫槽後,與上述充放電試驗同樣以0.4mA/cm2的電流密度和0V至3.5V的範圍的充電電壓下進行5次充放電測試來獲得放電容量。之後,返回到60℃的恆溫器並重新開始連續充電測試,並且進行測試直到連續充電測試時間的總和達到2000小時。 Next, a continuous charge test (constant current and constant voltage continuous charge test) was performed in a constant temperature bath at 60 ° C. with a charge current of 0.4 mA / cm 2 and a voltage of 3.5 V using a charge and discharge test device. Specifically, after charging is stopped for a predetermined time during the charging period, and the battery is transferred to a 25 ° C constant temperature bath, the current density of 0.4 mA / cm 2 and the charging voltage in the range of 0V to 3.5V are similar to the above-mentioned charge-discharge test. Next, 5 charge and discharge tests were performed to obtain the discharge capacity. After that, return to the thermostat at 60 ° C and restart the continuous charging test, and perform the test until the total of the continuous charging test time reaches 2000 hours.
結果得到的放電容量改善率如表1所示。放電容量改善率定義為,相對於定電流定電壓連續充電測試開始之前的放電容量,定電流定電壓連續充電試驗後的放電容量維持率變為80%以下的充電時間的壽命,並將後述的比較例1中的壽命的時間(2050小時)標準化為100。亦即,使用沒有進行氮摻雜處理的活性碳作為負極活性物質的場合的比較例1是標準化為100。 The resulting improvement in discharge capacity is shown in Table 1. The improvement rate of the discharge capacity is defined as the life of the charge time after the constant capacity constant-voltage constant-charge test is 80% or less of the discharge capacity before the constant-current constant-voltage continuous charge test is started. The life time (2050 hours) in Comparative Example 1 was normalized to 100. That is, Comparative Example 1 in a case where an activated carbon that has not been subjected to a nitrogen doping treatment is used as a negative electrode active material is standardized to 100.
[實施例2] [Example 2]
除了通過改變活性碳的氮摻雜處理時間(在升溫後保持氨氣流通的同時並維持在800℃的時間)從5分鐘改變為120分鐘,來改變活性碳的N/C比率(氮與碳的比率)之外,製作與實施例1相同的2032型鈕扣電池,並進行相同的評價。 In addition to changing the nitrogen doping treatment time of the activated carbon (the time to maintain the ammonia gas flow after heating and maintain it at 800 ° C) from 5 minutes to 120 minutes, the N / C ratio of activated carbon (nitrogen to carbon Except for the ratio), the same 2032-type button battery as in Example 1 was produced, and the same evaluation was performed.
結果得到的放電容量改善率如第1圖的圖表所示。該圖表的橫坐標表示N/C比率(氮與碳的比率,at%:原子組成百分比),圖表的縱坐標表示放電容量改善率(%)。 The obtained discharge capacity improvement rate is shown in the graph in FIG. 1. The abscissa of the graph represents the N / C ratio (the ratio of nitrogen to carbon, at%: atomic composition percentage), and the ordinate of the graph represents the discharge capacity improvement rate (%).
氮摻雜的效果開始出現在0.7at%,並且效果在1.0at%以上時增加,並且在2.0at%以上保持恆定。由該結果可知,N/C比率最優選為2.0at%以上及3.0at%以下。 The effect of nitrogen doping began to appear at 0.7 at%, and the effect increased when it was above 1.0 at%, and remained constant above 2.0 at%. From this result, it is found that the N / C ratio is most preferably 2.0 at% or more and 3.0 at% or less.
[實施例3] [Example 3]
除了使用大阪氣體化學股份公司製造的人造石墨(商品名:MCMB6-10)作為正極活性物質以外,製備與實施例1同樣的2032型鈕扣電池,並進行同樣的評價。 A 2032-type button battery was prepared and evaluated in the same manner as in Example 1, except that artificial graphite (trade name: MCMB6-10) manufactured by Osaka Gas Chemical Co., Ltd. was used as the positive electrode active material.
[比較例1] [Comparative Example 1]
除了使用由關西熱化學股份公司製造的未經氮摻雜處理的活性碳(產品名稱:MSP-20)作為負極活性物質之外,製備類似於實施例1的2032型鈕扣電池,並進行同樣的評價。 A 2032 type button battery similar to Example 1 was prepared except that activated carbon (product name: MSP-20) without nitrogen doping treatment manufactured by Kansai Thermochemical Co., Ltd. was used as a negative electrode active material, and the same was performed. Evaluation.
與使用未經氮摻雜處理的活性碳作為負極活性物質的比較例1相比,使用氮摻雜活性碳作為負極活性物質的實施例1將放電容量維持率提高8%。再者,除了使用摻氮活性炭作為負極活性物質之外,更使用不含菱形晶體的人造石墨作為正極活性物質的實施例3表現出將放電容量維持率提高7%,所以在任何一種情況下都可以證實氮摻雜處理的效果。 Compared with Comparative Example 1 using activated carbon without nitrogen doping treatment as the negative electrode active material, Example 1 using nitrogen doped activated carbon as the negative electrode active material improved the discharge capacity retention rate by 8%. Furthermore, in addition to the use of nitrogen-doped activated carbon as the negative electrode active material, Example 3, which uses artificial graphite without rhombic crystals as the positive electrode active material, shows that the discharge capacity maintenance rate is increased by 7%, so in any case The effect of the nitrogen doping process can be confirmed.
[實施例4] [Example 4]
除了2000小時連續充電試驗(定電流定電壓連續充電試驗)的充電電壓的範圍為3.6V至4.0V之外,進行與實施例1相同的評價。 The same evaluation as in Example 1 was performed except that the range of the charging voltage for the 2000-hour continuous charging test (constant current and constant voltage continuous charging test) was 3.6V to 4.0V.
就其結果,根據所得到的放電容量與平均放電電壓計算出能量(Wh),將結果示於表2。表2中,顯示了實施例4的能量通過比較例1進行標準化而獲得的值。此時,比較例1的結果標準化為100。 From the results, the energy (Wh) was calculated from the obtained discharge capacity and the average discharge voltage, and the results are shown in Table 2. Table 2 shows values obtained by normalizing the energy of Example 4 by Comparative Example 1. At this time, the result of Comparative Example 1 was normalized to 100.
另外,由連續充電試驗(定電流定電壓連續充電試驗)獲得的放電容量改善率示於第2圖中。圖表的橫軸表示連續充電試驗中的充電電壓(V),圖表的縱軸表示放電容量改善率(%)。 The improvement rate of the discharge capacity obtained by the continuous charge test (constant current and constant voltage continuous charge test) is shown in FIG. 2. The horizontal axis of the graph represents the charging voltage (V) in the continuous charging test, and the vertical axis of the graph represents the improvement rate (%) of the discharge capacity.
作為氮摻雜的效果,預計可減少下述情形:由於電解液的分解產生的氣體的情形;活性碳的表面被電解質分解產物覆蓋而使得比表面積減小及容量降低的情形;或由於活性碳本身的分解引起的劣化也會降低還原電位的情形。特別是由於在高溫下的劣化顯著,因此在60℃的2000小時連續充電試驗中評價充電電壓的變化。 As the effect of nitrogen doping, it is expected to reduce the following cases: the case of gas generated due to the decomposition of the electrolytic solution; the case where the surface of the activated carbon is covered with the decomposition products of the electrolyte to reduce the specific surface area and the capacity; or the activated carbon The degradation caused by the decomposition itself also reduces the reduction potential. In particular, since deterioration at high temperatures is significant, the change in charging voltage was evaluated in a 2000-hour continuous charging test at 60 ° C.
其結果如第2圖所示,相對於使用未經氮摻雜的活性碳作為負極活性材料的比較例1而言,放電容量改善率增加,直到充電電壓達到3.8V。此後,雖然放電容量降低直到充電電壓達到4.0V,但放電容量維持率仍高於比較例1。 As a result, as shown in FIG. 2, the improvement rate of the discharge capacity was increased as compared with Comparative Example 1 in which activated carbon that was not doped with nitrogen was used as a negative electrode active material, until the charging voltage reached 3.8V. After that, although the discharge capacity was reduced until the charging voltage reached 4.0 V, the discharge capacity retention rate was still higher than that of Comparative Example 1.
根據這些結果,發現即使通過氮摻雜使還原電位在朝減少的方向上發展,通過抑制電解液的分解或抑制活性碳自身的分解,也具有提高耐電壓的效果。基於第2圖中並且根據表2中的結果,發現耐電壓可以增加到使放電容量維持率變為最大的3.8V。 Based on these results, it has been found that even if the reduction potential develops in a decreasing direction by nitrogen doping, it is effective to increase the withstand voltage by suppressing the decomposition of the electrolytic solution or suppressing the decomposition of the activated carbon itself. Based on Figure 2 and based on the results in Table 2, it was found that the withstand voltage can be increased to 3.8 V that maximizes the discharge capacity retention rate.
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