TW200932676A - Method of manufacturing active carbon and electric double layer capacitor (EDLC) - Google Patents

Method of manufacturing active carbon and electric double layer capacitor (EDLC) Download PDF

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TW200932676A
TW200932676A TW97103664A TW97103664A TW200932676A TW 200932676 A TW200932676 A TW 200932676A TW 97103664 A TW97103664 A TW 97103664A TW 97103664 A TW97103664 A TW 97103664A TW 200932676 A TW200932676 A TW 200932676A
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Taiwan
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activated carbon
electric double
double layer
layer capacitor
carbonization
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TW97103664A
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Chinese (zh)
Inventor
Tatsuaki Yamaguti
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Sangyo Gijutsu Kenkyusho Co Ltd
Ibuki Susumu
Su Kou Chang
Fukui Osamu
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Application filed by Sangyo Gijutsu Kenkyusho Co Ltd, Ibuki Susumu, Su Kou Chang, Fukui Osamu filed Critical Sangyo Gijutsu Kenkyusho Co Ltd
Priority to TW97103664A priority Critical patent/TW200932676A/en
Publication of TW200932676A publication Critical patent/TW200932676A/en

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    • 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
    • Y02E60/13Energy storage using capacitors

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  • Electric Double-Layer Capacitors Or The Like (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

This invention provides an optimum active carbon required for an electric double layer capacitor (EDLC) having a large electrostatic capacity and low-priced material expenses or other similar purposes. The active carbon is produced by the following steps: a step of acquiring carbide by carbonizing raw materials obtained from bagasse produced in Okinawa or other regions (especially for the integument part obtained by separating the core part and the rind part of the foregoing bagasse), and a step of performing alkali activation for the foregoing carbide.

Description

200932676 九、發明說明: 【發明所屬之技術領域】 本發明係關於一種比表面積大的活性碳之製造方法。 此種活性碳係為電雙層電容器的分極性電極之主成份’亦 可供其他類似用途之最佳應用。另外,本發明係關於一種 電雙層電容器之製造方法,該電雙層電容器係具備一對分 極性電極、於該對分極性電極之間所配置之分隔膜、與該 ❿ 對分極性電極各自接續之一對集電極、及與該對分極性電 極所接觸之電解質。 【先前技術】 以往’使用活性碳作為分極性電極之主成分之電雙層 電容器係為習知的事實。此種電雙層電容器,例如,曰本 特許第3330235號公報(專利文獻丨)所揭示,係具備介於 分隔膜兩侧對向配置的一對分極性電極、及於該對分極性 電極的外侧(亦即,上述分隔膜之相反侧面)設置的一對集電 ❹ 極。又,於以活性碳為主成份之分極性電極中含有電解液。 而電荷係於該電解液與上述一對分極性電極中之一對界面 間所產生之一對電雙層中蓄積。此外,於專利文獻1所述, 作為用於該電雙層電容器之分極性電極之活性碳,從苯酚 樹脂(phenol resin)取得之活性碳之性能,較將紙聚等纖維素 (cellulose)經碳化、活性化所獲得之活性碳之性能優良。於 專利文獻1揭示之發明係使用將紙基材料的苯酚樹脂層積 板粉碎再經碳化處理、以驗金屬虱氧化物進行活性化處理 而獲得之多孔質碳材料’作為電雙層電容器之分極性電極 200932676 主成分之活性礙。 另一方面,甘蔗渣(換言之,搾完蔗汁後的殘渣)為製糖 工場等充當熱源或發電用燃料’因無法完全處理,多數形 成廢棄物。又,該充當熱源或發電用燃料之無法完全處^ 的甘蔗渣’亦被利用於作為紙、土壤改良材及吸附材所用。 為使甘蔗渣能作為吸附材料使用,係藉由碳化、氣體活性 化或藥品活性化、等活性化處理製作。然而,所製成之吸 ® 附材的bet比表面積約為i,〇〇〇m2/g左右。又,甘嚴渣係 由具有毛細管形成之蜂巢狀構造之纖維質之堅硬外表皮部 份,及中心部之柔軟細胞所形成的芯部所構成。而關於^ 甘蔗渣芯部與外皮部分離後所取得之各部位(即指外皮部份 及芯部)獲得之活性碳,並無詳細之探討。 77 於專利文獻1所揭示的電雙層電容器,其分極性電極 活性碳之主要成伤係為紙基苯紛樹脂層積板。因此,該電 雙層電容器無法擁有較大的靜電容量,且原材料費用亦^_。 本發明係為解決上述的諸問題所產生的發明',其目的 為提供原材料費便宜,同時亦可獲較大靜電容量之^雙層 電容器用、及其他類似用途之最適當的活性碳(即,多孔質 【發明内容】 本發明之第1方面係關於活性碳製造 物或;他產地之甘簾逢所獲得之原材料二而 2 ϊΐί之步驟’及將上述的碳化物經鹼活化處理之步 驟。於此情況下,上述原材料係以使上述賴渣的芯部與 7 200932676 外表皮部份互相分離獲得之外表皮為佳。將上述原材料經 鹼活性化處理後獲得之活性碳之bet比表面積以 3,000〜3,5〇Om2/g的範圍為佳,以3,250〜3,400m2/g的範圍 為較佳。 又’本發明之上述第1方面’上述礙化物的碳化溫度 以673K〜1,073K的範圍為佳,以733K〜973K的範圍為較 佳。而上述鹼金屬活性化處理所使用的鹼,以氫氧化鈉、 〇 氫氧化鉀等金屬氫氧化物為佳。又,於上述鹼活性化處理 時,鹼比前述碳化物之重量比係以4〜9之範圍為佳,以5〜8 ,更佳。又,上述的鹼活性化處理溫度以之 範圍為佳,以9现〜1,223K之範圍為更佳。又,上述的驗 ' /舌性化溫度以較上述碳化溫度高100Κ〜300Κ範圍内為佳, 以高150Κ〜250Κ範圍内為承杜lLaL , χ 雙層電容器使用者為佳為更佳。此外’上述活性碳以供電 ® ^之間所配置之分隔膜、與;=電==電 _集電極、及與該對分極杻金f刀f性電極各自接續之-層電容器之製造方法中,F電極所接觸之電解質。於電雙 -極的主要成份是使用活性2的3分極性電極中最少有 或其他產地之甘蔗渣獲得妷,上述之活性碳係以沖繩產 驟,及以前述碳化物進彳-a原料進行碳化獲得碳化物之步 於本發明之上述第^大舌化之步驟獲得。 述甘蔗渣芯部與外皮部八面,上述原料以上述藉由使前 上述活性礙之電雙層容I取得之如述外皮部份為佳。而 ,以170〜195F/g之範圍為佳,以 8 200932676 PS-WOF/g之範圍為較佳。 以氮氧化鈉、錄化鉀等驗金屬卜氫氧化所使用的驗 於本發明的第一及第二任一方面,住。 化物及上述活性礙當中的任何的i種、2種述:2碳 部,可採闕知適當的切斷步驟及/或 ^種全 驟來進行輯鐵柄•碎m 步 ❹ 破,::時,亦可省略此等切斷步驟及粉iii要切斷、 精由本發明’可以價廉的原材料及 驟’提供比表面積大且靜電容 」岭的氣乂步 專利範圍第2項至第4項…以申請 可提供更大靜絲4之活至^8_^_之發明, 項相關之路b日、,你—以 又藉申清專利範圍第10 原料費及相對簡易的製程,可提 電雙層電容量大的電雙層電容器。又,以 量^大的雷雔Π相關之發明,可進一步提供電雙層容 之發明:j曰電容器。又’以申請專利範圍第12項相關 層ΐ容器:"供電雙層電容量相當大,極具實用性之電雙 【實施方式】 雷簪二就本發明應用於電雙層電容器的實施例分為 I器全體之概略結構,(2)分極性電極的製造方 孔質碳素之特性試驗等項目,依第一圖至第十圖 1.電雙層電容器全體之概略結構 於本發明之-實施例之電雙層電容器1#第一圖及第 200932676 二圖所示,係具備經由分隔膜2配置的上下一對之分極性 電極3、4,及於此上下一對之分極性電極3、4的外側(亦 即,分隔膜2的相對侧面)設置之上下一對的集電極5、6。 此等層積體2至6係被收納入由適當的合成樹脂或其他材 料所製成的長方體形等之收納盒7中。此外,因於收納盒7 内係填充適當的電解液(換言之,電解質),分極性電極3、4 中,亦含有上述之電解液,且電荷係蓄積於此電解液及上 下一對之分極性電極3、4上下之界面上所產生之上下一對 的電雙層中。 如第一圖及第二圖所示,分隔膜2可為較收納盒7的 内周圍小一點、近似長方形、厚度薄之片狀。又,分隔膜2 的材質可為濾紙等紙質,纖維素(Cellul〇se)、玻璃纖維等 織布。上下-對之分極性電極3、4係以較分隔膜2小 二各自由活性碳等之多孔性碳素組成, 隹分極性電極的製造方法」中詳細說明。 此等上下二==55、: ’可為厚度薄之片狀所構成。 同形狀但尺寸較:;、之近似長圍大約 =5二6=上長;-對之集電二 == 之端子部二,形之片狀之上下4 的電方:其他導電性==,、6 第—圖及第二圖所示之上下一對的分極性電極 方形、厚度薄之片狀構成…前述上下-對: 其 此 3、4 10 200932676 可由以下詳述之方式所獲得之活性碳(即,多孔性碳素)加入 碳黑(Carbon black,由Sigma · Aldrich公司製造)之導電劑 及PTPE(聚四氟乙烯樹脂,Sigma. Aldrich公司製造)之粘 結劑,以重量比為如8:1:1混練後,充填入模型加壓成形, 製得如第一圖及第二圖所示之形狀。 於製造上述的活性碳時,原料來源為沖繩產之甘蔗 渣。該甘蔗渣係由堅硬的外表皮部份及柔軟細胞所組成的 φ 芯部兩種部位所構成,其重量比為約18 : 7。於本實施例中 係各自使用使上述甘蔗渣之芯部與外表皮部份分離後獲得 之这部、外表皮部分、及芯部與外表皮部分未分離前狀態 • 之甘蔗渣(即,芯部與外表皮部份一體化時的狀態,在本文 中以「芯部+外表皮部」或「芯+外皮」表示)三種類之原 料。 上述3種類之原料各自經24小時乾燥後,放入石英管 内的白金坩堝中,例如在氦氣流通下(例如流量約 40ml/min)’以例如5K/min的昇溫速度,昇溫至例如973K, Ο 於該溫度進行例如約1小時之碳化。於此種條件下所獲得 之3種碳化物(換言之,測試原料),各自進行下述的驗處理 (換s之,驗活化)。此時,所使用之活化劑,例如氫氧化納 (和光純藥公司製,日本實驗級特級)。此鹼處理係由使氣氧 化納以對l.Og之碳化物重量比為〇·〗至8.0方式調製而成之 水溶液中(例如約30ml中),攪拌約例如1小時進行。於授 拌後將此三種類試料,移至石英管内之白金坩禍中,以例 如5K/min之昇溫速度,昇溫至約例如ι.〇73Κ,且在該溫度 下保持例如1小時。經此種鹼活化後之三種類之測試原二 200932676 (換5之’活性碳),以純水或稀釋塩酸洗淨至洗淨後之pH 值約為7附近為土。 如上迷所製造之三種類的活性碳各自進行熱真空乾 燥。然後’此三種類的活性碳各自與前述例如碳黑(Sigma · Alderich 公司製)、例如 PTFE (Sigma · Aldrich 公司製),以 重量比為8:1:1之方式混練。接著’將這3種類的混練物各 自充填於模具經加壓成形,製造第一圖及第二圖所示之形 狀’可分別製造出3種類的分極性電極。又,於本文中, 上述活性碳(同樣也適用於分極性電極或活性碳電極)之製 造方法’採用甘蔗渣之芯部製造之活性碳(同樣邡適用於分 電極或活性碳電極)為具體例1 ;採用甘蔗渣的外表皮 邻伤製造之活性碳(分極性電極或活性碳電極亦然)為具體 例^2,採用甘蔗渣(換言之,芯部+外表皮部)製造之活性碳 (分極性電極或活性碳電極亦然)為具體例3。 3.活性碳之特性試驗 於前項 ❹ 厶分極性電極之製造方法」中以具體例丨至3 所製造之3種類的多孔性碳素(換言之,活性碳)進 之特性試驗,將前述3種類的混練物,各自充填〇 ,、 =13mm的三個模型中,經加壓成形成紐扣形狀H 、此3種類的鈕扣形體壓附於,例如用鈦篩網(丁1边 的集電體’即可製作出3種類試驗用之活性碳電梭 此互相比較此3種_活性碳電極之特性。 _:要以破素之特性實驗」’係依"下⑷項至 ⑷多孔性石炭素(換言之,活性碳)之細孔特性係利用 12 200932676 77K下定容之氮氣吸著式細孔分佈測定裝 製,ASAP2020)測試。(此時,微孔的容積係由MP 計算之,又,中孔(mes〇p〇re)容積則由BJH法解析 斤 ⑻活性碳的表面採用掃描式電子顯微 ⑷於元素分析時,以碳素、氮、氮 ^觀察晉 (YANAC〇 分析工業社製,YANACO CHN Corder 置 ❹ ⑩ 分別測定出石反、氫及氮的含有量,再將全量減 含有量之值即為氧氣之含量,及 之3種 (d)電雙層容量係使用3極式電池測試,(此時 極為上述3種賴活性碳電極(具_丨至3)之巾的任 種’對極則使用作用極6倍重量之活性碳電極(具體例 3中之任一),參考電極則使用飽和甘汞(Calomel)電極。雷 5〇〇ml° ^ 各自认於正負方向的過程中之定電流(例如1〇〇m 的電位與時_變化曲線斜率依下式計算求出。 C=IxAT/(V2 ~V1)=ixat/AV I : 一定電流200932676 IX. Description of the Invention: [Technical Field of the Invention] The present invention relates to a method for producing activated carbon having a large specific surface area. This activated carbon is the main component of the bipolar electrode of the electric double layer capacitor' and is also suitable for other similar applications. Further, the present invention relates to a method of manufacturing an electric double layer capacitor comprising a pair of polarization electrodes, a separation film disposed between the opposite polarity electrodes, and each of the ❿ 极性 polarity electrodes One of the pair of collectors and the electrolyte in contact with the pair of polar electrodes. [Prior Art] Conventionally, an electric double layer capacitor using activated carbon as a main component of a polar electrode is a conventional fact. For example, the electric double-layer capacitor includes a pair of sub-polar electrodes disposed opposite to each other on both sides of the separation film, and a bipolar electrode disposed on the opposite side of the separation film, as disclosed in Japanese Patent No. 3330235 (Patent Document No.). A pair of collector electrodes provided on the outer side (i.e., opposite sides of the above separation film). Further, an electrolyte solution is contained in a polar electrode containing activated carbon as a main component. The electric charge is accumulated in one of the pair of electric double layers generated between the electrolyte and one of the pair of bipolar electrodes. Further, as described in Patent Document 1, as the activated carbon for the polarization electrode of the electric double layer capacitor, the performance of the activated carbon obtained from the phenol resin is higher than that of the cellulose obtained by the paper. The performance of activated carbon obtained by carbonization and activation is excellent. In the invention disclosed in Patent Document 1, a porous carbon material obtained by pulverizing a phenol resin laminated plate of a paper-based material and then carbonizing the metal cerium oxide for activation treatment is used as an electric double layer capacitor. Polar electrode 200932676 The active component of the main component. On the other hand, sugar cane bagasse (in other words, the residue after the cane juice is squeezed out) serves as a heat source or a fuel for power generation for a sugar plant, etc., and most of the waste is formed because it cannot be completely treated. Further, the bagasse which is a heat source or a fuel for power generation which cannot be completely used is also used as a paper, a soil improving material, and an adsorbing material. In order to use bagasse as an adsorbent material, it is produced by carbonization, gas activation, drug activation, and the like. However, the bet specific surface area of the produced suction material is about i, about 2m2/g. Further, the slag is composed of a hard outer skin portion of a honeycomb structure having a honeycomb structure formed by a capillary, and a core portion formed by soft cells at the center. The activated carbon obtained from the various parts (ie, the outer skin portion and the core) obtained after the separation of the core and the outer skin of the bagasse has not been discussed in detail. 77. In the electric double layer capacitor disclosed in Patent Document 1, the main component of the bipolar electrode active carbon is a paper-based resin laminated plate. Therefore, the electric double layer capacitor cannot have a large electrostatic capacity, and the cost of raw materials is also ^. The present invention is an invention for solving the above problems, and the object thereof is to provide a double-layer capacitor having a low raw material cost and a large electrostatic capacity, and the most suitable activated carbon for other similar uses (ie, , porous content [Summary of the Invention] The first aspect of the present invention relates to a step of producing an activated carbon or a raw material obtained from the production of the same, and a step of activating the above-mentioned carbide by alkali activation. In this case, the raw material is obtained by separating the core of the slag and the outer skin portion of 7 200932676 to obtain an outer skin. The bet specific surface area of the activated carbon obtained by alkali-activated the above raw material. The range of 3,000 to 3,5 〇Om 2 /g is preferably in the range of 3,250 to 3,400 m 2 /g. Further, the above first aspect of the present invention has a carbonization temperature of 673 K to 1,073 K. The range is preferably 733 K to 973 K. The alkali used for the alkali metal activation treatment is preferably a metal hydroxide such as sodium hydroxide or cesium hydroxide. Chemical When the treatment, the weight ratio of the alkali to the carbide is preferably in the range of 4 to 9, more preferably 5 to 8. Further, the above-mentioned alkali activation treatment temperature is preferably in the range of 9 to 1, The range of 223K is better. Moreover, the above-mentioned test / tongue temperature is preferably in the range of 100 Κ to 300 高 higher than the above carbonization temperature, and is in the range of 150 Κ to 250 高 in height, which is the user of double-layer capacitors. It is better to be better. In addition, the above-mentioned activated carbon is supplied between the power supply and the partition film, and the electric current is connected to the pair of electrodes. In the manufacturing method of the layer capacitor, the electrolyte contacted by the F electrode. The main component of the electric double-pole is obtained from the bagasse of at least the other 3 or more polar electrodes of the active 2, and the activated carbon is Okinawa. The production step and the step of carbonizing the carbide into the cerium-a raw material to obtain the carbide are obtained in the above-mentioned step of the smear of the present invention. The core of the bagasse and the outer skin are eight sides, and the above raw materials are borrowed as described above. The outer skin portion obtained by the electric double layer capacity I of the above-mentioned active Preferably, the range is 170~195F/g, and the range of 8200932676 PS-WOF/g is preferred. The test for the use of sodium hydroxide, potassium, etc. According to any one of the first and second aspects of the present invention, any one or two of the above-mentioned active substances and the above-mentioned active substances: 2 carbon parts, which can be appropriately cut and/or fully To carry out the series of iron handles, the broken m steps, and the:::, the cutting steps can be omitted, and the powder iii should be cut off. The invention can provide a large specific surface area and a static capacitance. Ling's patented scope of the second to fourth items... to apply for the invention of a larger static wire 4 to ^8_^_, the relevant road b, you - to borrow Shen Qing The patented range of 10 material costs and a relatively simple process can be used to provide electric double-layer capacitors with large double-layer capacitance. Further, the invention of the electric double layer can be further provided by the invention relating to the Thunder which is large in size: j曰 capacitor. In addition, the patent application scope 12 related layer container: " power supply double-layer capacity is quite large, very practical electric double [implementation] Thunder two on the embodiment of the present invention applied to electric double-layer capacitor It is divided into a schematic structure of the whole of the I, and (2) a test of the characteristic of the porous carbon of the polar electrode, and the like. According to the first to the eleventh, the schematic structure of the entire electric double layer capacitor is used in the present invention. - The electric double layer capacitor 1# of the embodiment and the second figure of 200932676 show a pair of upper and lower polarity electrodes 3 and 4 disposed via the separator 2, and a pair of upper and lower polarity electrodes The outer sides of 3, 4 (i.e., the opposite sides of the separation film 2) are provided with a pair of upper and lower collectors 5, 6. These laminates 2 to 6 are housed in a storage box 7 having a rectangular parallelepiped shape or the like made of a suitable synthetic resin or other material. Further, since the storage case 7 is filled with an appropriate electrolyte (in other words, an electrolyte), the above-mentioned electrolyte solution is also contained in the polarization electrodes 3 and 4, and the charge is accumulated in the electrolyte and the polarity of the upper and lower electrodes. The upper and lower pairs of electrodes 3, 4 are formed in the upper and lower pairs of electric double layers. As shown in the first and second figures, the separation film 2 may be a sheet having a smaller size, a substantially rectangular shape, and a thinner thickness than the inner circumference of the storage case 7. Further, the material of the separator 2 may be paper such as filter paper, cellulose (Cellul) or glass fiber. The upper and lower polarizing electrodes 3 and 4 are each composed of a porous carbon which is smaller than the separator 2 and each of which is composed of porous carbon such as activated carbon, and a method for producing a polar electrode. These upper and lower two == 55, : ' can be formed into a sheet having a thin thickness. The same shape but the size is:;, the approximate length is about = 5 2 6 = upper length; - the collector 2 of the collector 2 == the second part of the shape, the upper part of the shape of the sheet 4: other conductivity == , and the first and second pairs of the polar electrodes are arranged in a square shape and the thickness is thin. The above-mentioned upper and lower-pairs: 3, 4 10 200932676 can be obtained by the following detailed description. Activated carbon (ie, porous carbon) is added to a carbon black (Carbon black, manufactured by Sigma Aldrich) conductive agent and a binder of PTPE (polytetrafluoroethylene resin, manufactured by Sigma. Aldrich) in a weight ratio. After kneading as in 8:1:1, the model is press-formed to obtain a shape as shown in the first figure and the second figure. In the production of the above activated carbon, the raw material source is the sugar cane slag produced by Okinawa. The bagasse is composed of a hard outer skin portion and a soft core composed of two core portions, and has a weight ratio of about 18:7. In the present embodiment, each of the outer skin portion obtained by separating the core portion of the bagasse from the outer skin portion and the bagasse (ie, the core) in the state before the core portion and the outer skin portion are not separated are used. The state in which the part is integrated with the outer skin part is referred to herein as "core + outer skin" or "core + outer skin". Each of the above three types of raw materials is dried for 24 hours, and then placed in a platinum crucible in a quartz tube, for example, under a helium gas flow (for example, a flow rate of about 40 ml/min), and the temperature is raised to, for example, 973 K at a temperature increase rate of, for example, 5 K/min.碳 is carbonized at this temperature, for example, for about one hour. The three types of carbides obtained under such conditions (in other words, test materials) were subjected to the following treatments (for s, activation). In this case, an activator to be used is, for example, sodium hydroxide (manufactured by Wako Pure Chemical Industries, Ltd., Japan Experimental Grade). This alkali treatment is carried out in an aqueous solution (e.g., about 30 ml) prepared by oxidizing a gas to a weight ratio of 1.0 g to a weight of 1.0 g, and stirring for about 1 hour. After the mixing, the three kinds of samples were transferred to a platinum in a quartz tube, and the temperature was raised to about, for example, ι.〇73Κ at a temperature rising rate of, for example, 5 K/min, and maintained at the temperature for, for example, 1 hour. After the activation of the alkali, the three types of test raw materials 200932676 (for 5 activated carbon) were washed with pure water or diluted citric acid until the pH value after washing was about 7 soil. The three types of activated carbons produced as described above were each subjected to thermal vacuum drying. Then, each of the three types of activated carbon is kneaded in a weight ratio of 8:1:1 to the above-mentioned, for example, carbon black (manufactured by Sigma Alderich Co., Ltd.), for example, PTFE (manufactured by Sigma Aldrich Co., Ltd.). Then, the three kinds of kneaded materials were each filled in a mold and subjected to press molding to produce the shapes shown in the first figure and the second figure. Three kinds of polarization electrodes were respectively produced. Further, in the present invention, the above-mentioned method for producing activated carbon (also applicable to a polar electrode or an activated carbon electrode) is made of activated carbon produced by the core of bagasse (also applicable to a split electrode or an activated carbon electrode). Example 1; Activated carbon (also referred to as a polar electrode or an activated carbon electrode) produced by the outer skin adjacent injury of bagasse as a specific example 2, using activated carbon produced from bagasse (in other words, core + outer skin) The same applies to the case of the polar electrode or the activated carbon electrode. 3. Characteristics of activated carbon In the first method, the three types of porous carbon (in other words, activated carbon) produced by the specific example 丨 to 3 are tested in the characteristics of the activated carbon. The kneaded materials, each of which is filled with 〇, and =13 mm, are pressed to form a button shape H, and the three types of button-shaped bodies are pressed, for example, with a titanium mesh (a collector of a side of the side) Three kinds of activated carbon electric shuttles for testing can be produced, and the characteristics of the three kinds of _activated carbon electrodes are compared with each other. _: Experiment with the characteristics of the breaking factor" "By Dependence" (4) to (4) Porous Carboniferous (In other words, the pore characteristics of the activated carbon) were tested by a nitrogen sorption type pore distribution measurement with a constant volume of 12 200932676 77K, ASAP2020). (At this time, the volume of the micropores is calculated by MP, and the volume of the mesoporous (mes〇p〇re) is analyzed by the BJH method. The surface of the activated carbon is scanned by scanning electron microscopy (4). Carbon, nitrogen, nitrogen ^ observation Jin (YANAC〇 Analytical Industrial Co., Ltd., YANACO CHN Corder placed 10 to determine the content of stone, hydrogen and nitrogen, respectively, and then the total amount of reduced content is the oxygen content, and The three types of (d) electric double-layer capacity are tested using a 3-pole battery. (At this time, any of the above three kinds of activated carbon electrodes (with _丨 to 3) are used. The weight of the activated carbon electrode (any one of the specific examples 3), the reference electrode uses a saturated calomel (Calomel) electrode. Ray 5 〇〇 ml ° ^ each recognizes the constant current in the process of positive and negative directions (for example, 1 〇 The potential of 〇m and the slope of the time-change curve are calculated according to the following equation: C=IxAT/(V2 ~V1)=ixat/AV I : a certain current

Vi·充電或放電開始電位 V2 :充電或放電終了電位 △T·充電或放電所需的時間 •^先,就作為上述3種類活性碳原料之甘(即,芯 表皮部)及其他各部位(即,「芯部」及「外表 ,,說明:甘薦法之元素分析值,如下表i所示。即, 被、虱及氧各το素含有量,無論外表皮部或料均大致相 同。但灰份的含有量於芯部較外表皮部擁有較高值(約 13 200932676 5.8wt%) 元素分; H-(d. a. f.) [wt%] ~~· _ 莫耳比[-] 灰分(d. b)[wt%] C H N 〇(差) H/C O/C 心+外表皮 (7:18) 0.6 47.6 5.7 0.2 46.5 1.44 0.73 芯 5.8 48.5 5.9 0.5 45.2 1.45 0. 70 外表皮 1.9 48.3 5.8 0.2 45.6 1.45 0.71 d. a. f. :無水無灰之基準 d. b : 乾燥量基準 一第三圖(A)係為甘蔗渣芯部之SEM顯微組織圖。又,第 •^圖(B)係為甘嚴渣的外表皮部份之SEM顯微組織圖。 = 知外表皮部具有多數來源為孔徑約ι〇_之毛細Vi·Charging or discharging start potential V2 : Charging or discharging end potential ΔT·Time required for charging or discharging • First, as the above-mentioned three types of activated carbon raw materials (ie, core skin portion) and other parts ( That is, the "core" and the "appearance" indicate that the elemental analysis value of the ginseng method is as shown in the following table i. That is, the content of each of the sputum, the sputum, and the oxygen is substantially the same regardless of the outer skin or the material. The content of the part has a higher value (about 13 200932676 5.8wt%) than the outer part of the core; H-(daf) [wt%] ~~· _ Moer than [-] ash (d. b) ) [wt%] CHN 〇 (poor) H/CO/C heart + outer skin (7:18) 0.6 47.6 5.7 0.2 46.5 1.44 0.73 core 5.8 48.5 5.9 0.5 45.2 1.45 0. 70 outer skin 1.9 48.3 5.8 0.2 45.6 1.45 0.71 Daf: waterless ash-free d. b: dry basis. The third figure (A) is the SEM micrograph of the core of the bagasse. In addition, the figure (B) is outside the slag. SEM micrograph of the epidermis. = The external epidermis has a capillary with a majority of pore sizes of about ι〇_

I”相對的,由第三圖⑷可知芯部並無具備如外皮 般多之空洞,係為粉末狀。 W rBL ⑩ 接著,再針對甘蔗渣及其各部位經碳 說明,2種原料(即,甘蔗渣的“钟,,及7表之 約W3K〜973K之溫度範圍中進行碳化。第四圖係 甘嚴潰的芯部及外表皮部之碳化溫之車、及瑞 任Γ種,若碳化溫度高於_心其產率會 ;:Γ=?Γ73Κ時產率則幾乎維持於-定數In contrast, in the third figure (4), it is known that the core does not have as many voids as the outer skin, and is in the form of a powder. W rBL 10 Next, the carbonaceous material and various parts thereof are described by carbon, and two kinds of raw materials (ie, Carbonized in the temperature range of W3K~973K of the bagasse, and the carbonized temperature of the core and the outer skin of the stagnation, and the ruthenium The carbonization temperature is higher than the _ heart yield;; Γ =? Γ 73 Κ when the yield is almost maintained at - fixed

化溫=上⑽碳 後,維持於一宕盔佶 匕則田奴化溫度尚於約873K 97;K#^ ^ 具故3有1均為90%以上。 200932676 此現象係因由芯部或外表皮部的熱分解導致水及二氧化碳 因脫氫及脫氧所致。又,此時所獲得碳化物的bet比表面 積於碳化溫度約為973K時約為20m2/g。因此,本發明就實 用性觀點而言,碳化溫度在673K以上、1073K以下為佳, 又以773K以上、973K以下為更佳。 由第四圖所述之特性可判斷碳化溫度對於甘蔗潰之芯After the temperature = upper (10) carbon, it is maintained at the same time. The temperature of the slain is still about 873K 97; K#^^ has 3 and 1 is more than 90%. 200932676 This phenomenon is caused by dehydrogenation and deoxidation of water and carbon dioxide due to thermal decomposition of the core or outer skin. Further, the bet specific surface area of the obtained carbide at this time was about 20 m 2 /g at a carbonization temperature of about 973 K. Therefore, in the present invention, the carbonization temperature is preferably 673 K or more and 1073 K or less, and more preferably 773 K or more and 973 K or less. From the characteristics described in the fourth figure, the carbonization temperature can be judged for the core of sugar cane

部及外表皮部之構造變化有相當大的影響。第五圖(A)係揭 示以甘蔗渣芯部作為原料,於碳化溫度約973K下碳化所獲 得之碳化物(具體例1)構造之SEM影像。第五圖(B)係揭示 以甘蔗渣外表皮部為原料,於碳化溫度973K下碳化所獲得 之碳化物(具體例2)構造之SEM影像。由第五圖(A)可=, 由芯部所獲得之碳化物與第三圖(A)所示維持原料狀態之芯 部幾乎保有同樣形狀。又,由第五圖(B)可知,由外表皮部 所得之碳化物與第三圖(B)所示之原料(即,碳化前之外表1 部)相比較,雖然可見因熱分解之脫氧導致毛細管構造崩壞 之部分,但仍幾乎保持與原料的構造相似之狀態。 接著,針對甘蔗渣及其他各部位經碳化後所獲得之 種類的碳化物,分別藉鹼活化後製成上述3種類之活性赛 =性分別說明。於第六圖係揭示了此3種類的活性碳名 ^生化溫度H)73K時,驗(具體而言,氣氧化納)之添加漫 比^物之重量比)與蕭比表面積及產率的關痛 L、圖5么’驗f加量對產率及臟比表面積之影響)。由第 ς圖可知’由芯部+外表皮部,芯部及外表皮部中任何一 添種類的活性碳,前述3種類的碳化物隨著驗 …1之日加,其各自的ΒΕΤ比表面積均有增加之趨勢。 15 200932676 又’於鹼添加量為6.0時,可獲得BET比表面積達3,0〇〇m2/ 以上^活性碳。以活性化溫度(於實用性觀點下)而言, 以較碳化溫度高出1〇〇κ以上、3〇〇κ&下為佳,以高出 以上、250K以下為更佳。因此,上述之活性化溫度,就你 用性觀點而言,以823K以上、1323以下為佳,以923K: ^ 上、1223K以下為更佳。 λ 於第七圖(Α)至第七圖係揭示了由甘蔗渣的芯部 獲得之活性碳(具體例1)之SEM影像。第七圖(A)係為給 加量為L7,BET比表面積為9〇lm2/g之狀況。第七圖= 係為鹼添加量為2·9,BET比表面積為16951112^之狀况。 '第七圖(C)係為鹼添加量為3.7,BET比表面積為2,ll3m2/° - 之狀況。又;第七圖(D)係為鹼添加量為6.5 , BET比表^ ,為3,120m2/g之狀況。由第七圖至第七圖(D)可知, 芯部所獲得之活性碳會隨著因鹼活化導致之bet比表面 增加,使構成活性碳之粒子之尺寸變小。對此,於第八圖认 至第八圖ff>)係揭示由甘蔗渣的外表皮所獲得之活性琰 ⑩ 體性2)的δΕΜ影像。第八圖(A)係為鹼添加量為丨〇, 比表面積為889m2/g之狀況。第八圖(Β)係為鹼添加量為 2.0,BET比表面積為之狀況。第八圖(c)係為& 添加量為3.0,BET比表面積為2,030m2/g之狀況。又,第 八圖(D)係為鹼添加量為6〇,BET比表面積為3,328m2/g之 狀况。由第八圖(A)至第八圖⑼可知,自外表皮部所獲得的 活性碳,會隨著因鹼活化導致之BET比表面積增加,雖然 毛細管構造多少有些崩壞,但還保有微小尺寸之毛細管構 造。而由外表皮部所獲得之活性碳,即使使其BET比表面 16 200932676 積增大,仍維持其毛細管構造。因此可知,於本發明就實 用性的觀點而言’驗比前述礙化物之重量比以4以上、9以 下為佳’以5以上、8以下為較佳。此外,本發明就實用性 的觀點而言,活性碳之BET比表面積以3,〇〇〇m2/g以上、 3,500m2/g以下為佳,以3,250m2/g以上、3,45〇m2/g以下為 更佳。The structural changes in the outer and outer skins have considerable influence. Fig. 5(A) shows an SEM image of the structure of the carbide (specification 1) obtained by carbonizing the core of the bagasse as a raw material at a carbonization temperature of about 973 K. Fig. 5(B) shows an SEM image of a carbide (Specific Example 2) structure obtained by carbonizing at the carbonization temperature of 973 K from the outer skin portion of the bagasse. From the fifth diagram (A), the carbide obtained from the core portion has almost the same shape as the core portion in the state of maintaining the raw material shown in Fig. 3(A). Further, as is understood from the fifth diagram (B), the carbide obtained from the outer skin portion is compared with the material shown in the third diagram (B) (i.e., the portion before the carbonization), although deoxidation due to thermal decomposition can be seen. The part that causes the capillary structure to collapse, but still maintains a state similar to the structure of the raw material. Next, the types of carbides obtained by carbonization of bagasse and other parts are activated by alkali to prepare the above three types of activity. In the sixth figure, the three types of activated carbons, biochemical temperature H) 73K, the specific gravity ratio of the specific gravity of the test (specifically, gas oxidized nano) and the specific surface area and yield are shown. Guan Guan L, Figure 5, 'the effect of f-addition on yield and dirty specific surface area. It can be seen from the figure that 'the activated carbon from the core + outer skin, the core and the outer skin is added. The above three types of carbides are added to the surface of the test. There is an increasing trend. 15 200932676 Further, when the amount of alkali added is 6.0, a BET specific surface area of 3,0 〇〇m 2 /more or more activated carbon can be obtained. The activation temperature (in view of practicality) is preferably 1 〇〇 κ or more and 3 〇〇 κ 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 Therefore, the above-mentioned activation temperature is preferably 823 K or more and 1323 or less, and more preferably 923 K: ^ or 1223 K or less from the viewpoint of usability. λ From the seventh (Α) to the seventh diagrams, SEM images of activated carbon obtained from the core of bagasse (Specific Example 1) are disclosed. The seventh diagram (A) shows a case where the amount of addition is L7 and the BET specific surface area is 9 〇lm 2 /g. Fig. 7 is a condition in which the amount of alkali added is 2·9 and the BET specific surface area is 16951112^. The seventh figure (C) is a case where the amount of alkali added is 3.7 and the BET specific surface area is 2, ll3 m 2 /° -. Further, the seventh figure (D) is a case where the amount of alkali added is 6.5 and the BET ratio is ^, which is 3,120 m 2 /g. As is apparent from the seventh to seventh figures (D), the activated carbon obtained in the core increases the size of the bet which constitutes the activated carbon as the surface of the activated carbon increases as the alkali is activated. In this regard, it is recognized in the eighth figure to the eighth figure ff>) that the δΕΜ image of the activity obtained from the outer skin of bagasse is revealed. The eighth diagram (A) shows a case where the amount of alkali added is 丨〇 and the specific surface area is 889 m 2 /g. The eighth figure (Β) is a condition in which the amount of alkali added is 2.0 and the BET specific surface area is obtained. The eighth figure (c) is a case where the addition amount is 3.0 and the BET specific surface area is 2,030 m 2 /g. Further, Fig. 8(D) shows a case where the amount of alkali added is 6 Å and the BET specific surface area is 3,328 m 2 /g. From Fig. 8(A) to Fig. 8(9), it is known that the activated carbon obtained from the outer epidermis increases with the BET specific surface area due to alkali activation, and although the capillary structure somewhat collapses, it still retains a small size. Capillary construction. The activated carbon obtained from the outer epidermis maintains its capillary structure even if its BET is increased in proportion to the surface 16 200932676. Therefore, in the present invention, from the viewpoint of practicality, the weight ratio of the above-mentioned inhibitor is preferably 4 or more and 9 or less, and more preferably 5 or more and 8 or less. Further, in view of practicality, the present invention preferably has a BET specific surface area of activated carbon of 3, 〇〇〇m2/g or more and 3,500 m2/g or less, and 3,250 m2/g or more and 3,45 〇m2/ The following is better.

於第九圖係揭示上述3種類活性碳各自於77K之氣氣 吸附等溫曲線。由上述3種類的原料所獲得之bet比表面 積超過3,000m2/g之活性碳之氮氣吸附等溫曲線,依IUPAC (艮P ,International Union of Pure and Applied Chemistry)吸脫 附等溫曲線的分類為Π型。於第九圖中,P為吸附平衡壓, Po為飽和蒸氣壓。表2為於第九圖所揭示之氮氣吸附等溫 線經解析而計算出之細孔媒介變數。由表2可知,上述3 種類之活性碳中任何一種均可促進其中孔(Mes〇 p〇re)的發 達。 表2 原料 驗添加量 (g/g) 總表面積S (m2/g) S (m2/g) 總Vp Vp (cm2/g) 中孔 (cm3/g) 微孔 中孔 芯+外皮(7:18) 6.2 3343 2606 2.07 0.17 1.85 芯部 6.5 3120 2194 2.18 0.03 1.81 外表皮部 6.0 3328 “丨 2353 2.08 0.16 1.73 S . BET比表面積 Vp :細孔容積 接著說明具有高比表面積又具中孔多孔性之甘蔗渣活 性碳(即,由甘蔗渣所獲得之活性碳)的電雙層之特性,於第 17 200932676 十®係揭示上述3種類活性 性碳電極(具體例3)比較,於各;^2表皮部所獲得之活 電雙層容量。自外表皮部所^ 匕^面積均具有較高之 ❿ ⑩ 量之最高值麵在職喊碳電極的電雙層容 183F/g,較由芯部或芯部+外表口 3’,,仏時、約為 高出1〇〜2,§。因此,於 對此而古,於矣9私? 190;^以下為更佳。 種類(換言之,甘蔬渣之各二大,料 之存在。又,由活性碳之酸性官能以性特徵 起因之觀點而言,於擁有最高 層2層各篁增加之In the ninth figure, the gas-gas adsorption isotherm curves of the above three types of activated carbons at 77K are disclosed. The nitrogen adsorption isotherm curve of activated carbon having a specific surface area of more than 3,000 m 2 /g obtained from the above three types of raw materials is classified according to the IUPAC (International Union of Pure and Applied Chemistry) adsorption-desorption isotherm curve. Π type. In the ninth diagram, P is the adsorption equilibrium pressure and Po is the saturated vapor pressure. Table 2 shows the pore media variables calculated by analyzing the nitrogen adsorption isotherms disclosed in Figure 9. As can be seen from Table 2, any of the above three types of activated carbon promotes the development of pores (Mes〇p〇re). Table 2 Addition amount of raw materials (g/g) Total surface area S (m2/g) S (m2/g) Total Vp Vp (cm2/g) Medium pores (cm3/g) Microporous medium core + outer skin (7: 18) 6.2 3343 2606 2.07 0.17 1.85 Core 6.5 3120 2194 2.18 0.03 1.81 External skin 6.0 3328 "丨2353 2.08 0.16 1.73 S . BET specific surface area Vp : pore volume followed by high specific surface area and mesoporous porosity The characteristics of the electric double layer of bagasse activated carbon (i.e., activated carbon obtained from bagasse) are disclosed in the 17th 200932676 ten series to reveal the above three types of active carbon electrodes (specific example 3), respectively; The double layer capacity of the live electric layer obtained from the epidermis. From the outer epidermis, the area of the 匕^ area has a higher ❿10. The highest value of the surface is called the carbon electrode's electric double layer capacity 183F/g, compared to the core or Core + external port 3', when 仏, is about 1〇~2, §. Therefore, in this case, Yu 矣9 private? 190; ^ below is better. Type (in other words, sweet and vegetable The slag is the second largest, the existence of the material. In addition, from the point of view of the acidic characteristics of the activated carbon, it has the highest level of the two layers.

(-〇Hne Exchange CEC =氣值置 如由外表皮部 =二 ==:;。有二知, 部所獲得之活性破,因毛細管有皮 ==為促使外表皮部所獲得的活性di容 里曰大之原因。因此可判定,甘薦渣中, ^ 適為電雙層電容的分極性 電核之主要成 ❹ Φ 200932676 以上述所,例·兒明。然而,本發明非 本發明為亦可以於專利申請範圍記載之 述之實施2 行各歸正與變更。例如,於既 隔膜2、—對的長方形之形狀所構成,同時分 各自之集電極本體5a、6a均各* Μ!、集電極5、6的 然而,收納各7可修故太士各由近似長方形狀體所構成。 隔辑2、— “分極;電極3近爻圓及筒一形 ^自之集電極本體5a、6a各自:HI 5構:二 =’分隔膜2及一對的 : 形狀構成,同時將此分隔膜2 4:了由乍長 再卷繞而形成迴卷體,再置^ 電極3、4互相層積 此外’於既二=近=2納盒7中。 的各自拉出的電極,係作為該對^ 5&、6& 扑,與上述之-對的集電極本子部%、 上述拉出的電極亦可與集電c形。然而’ 體方式構成。 I體5a、以以分別不同之個 200932676 【圖式簡單說明】(-〇Hne Exchange CEC = gas value is set by the outer skin = two ==:; There are two knowledge, the activity obtained by the ministry is broken, because the capillary has skin == to promote the activity of the outer epidermis Therefore, it can be determined that in the slag slag, ^ is the main component of the bipolar capacitor of the electric double layer capacitor Φ 200932676. It is also possible to correct and change the implementation of the description in the scope of the patent application. For example, it is formed by the shape of the rectangular shape of the diaphragm 2 and the pair, and the respective collector bodies 5a and 6a are respectively * Μ! However, the collectors 5 and 6 are respectively arranged to be composed of approximately rectangular bodies. The spacer 2, - "polarization; the electrode 3 is nearly rounded and the tube is shaped from the collector body 5a" , 6a each: HI 5 structure: two = 'separating film 2 and a pair: shape configuration, at the same time this separation film 24: re-winding from the length of the crucible to form a rewind body, and then set the electrode 3, 4 The layers are laminated to each other in the two adjacent = 2 nanocells 7. The electrodes that are pulled out are used as the pair of 5&, 6& The above -.% Of the portion of the book collector, said drawing electrode current collector and also a c-shaped configuration, however embodiment thereof 'I body 5a, to a respectively different drawings briefly described [200,932,676]

第一圖係為於本發明應用於電雙層電容器之實施例 時,該電雙層電容器全部之剖面概要立體圖。(實施例U 第二圖係為揭示於第一圖所示之電雙層電容器,省略 收納盒後之狀態之分解立體圖。(實施例υ +第三圖(Α)麵製造第_圖所示之分極性電極所使 甘嚴:查心部之SEM影像。(實施例1) ❹ ⑩ #第二圖(B)係為製造第—圖所示之分極性電極所使 甘庶渣外表皮部之SEM影像。(實施例J) ί四圖係為關於製造第-圖所示之分極性電極所使用 之甘藉ϋ料外表皮部之碳化溫度及碳化物的產率遍 元素組成之圖表。(實施例1) >、 第五圖⑷係為第三圖(Α)的甘 SEM影像。(實施例丨) 便的 第五圖(B)係為第二圖(B)的甘嚴潰外表皮部經碳 的SEM影像。(實施例1) 谈 ⑻所第H係為第五圖(A)所示之由甘蔗渣的芯部及第五圖 、㈣外表皮部,及糾+外表皮部各^ 二T碳之驗添加量與贿比表面積及產率之圖表ί 第七圖(Α)係為第五圖(八)中 =比表面積一之活性狀sem4“(= 第七圖(B)係為第五圖(A)中所示,由甘蔗 廳比表面積為之活性碳之 20 200932676 1) 第七圖(c)係為第五圖⑷中所示,由甘篇造芯部所 BET比表面積為2,ll3m2/g之活性碳之SEM影像 二侍 1 ) 、爲苑例 第七圖(D)係為第五圖(A)中所示’由甘蔗渣芯部 得,BET比表面積為3,120m2/g之活性碳之SEM影像。^ 施例1) y 。(實The first figure is a schematic perspective view of a cross section of the electric double layer capacitor in the embodiment of the present invention applied to an electric double layer capacitor. (Embodiment U) The second drawing is an exploded perspective view of the electric double layer capacitor shown in the first figure, and the state after the storage case is omitted. (Example υ + Third drawing (Α) surface manufacturing _ The polarity of the electrode is made to be strict: the SEM image of the core is found. (Example 1) ❹ 10 # The second figure (B) is the outer skin of the sorghum slag which is made by the polarity electrode shown in the figure. SEM image. (Example J) Figure 4 is a graph showing the carbonization temperature of the outer skin portion of the material used for the production of the polar electrode shown in Fig. - and the yield composition of the carbide. (Example 1) > The fifth figure (4) is the SEM image of the third figure (Α). (Example 丨) The fifth figure (B) is the second picture (B) SEM image of carbon on the outer skin. (Example 1) The H series in (8) is the core of bagasse and the fifth and (4) outer skins shown in Fig. 5(A), and Chart of each part of the epidermis ^ 2 T carbon and brittle specific surface area and yield ί The seventh figure (Α) is the fifth figure (eight) = specific surface area one active sem4 " (= seventh figure (B The system is shown in the fifth figure (A), the specific surface area of the sugar cane hall is activated carbon 20 200932676 1) The seventh figure (c) is shown in the fifth figure (4), by the ginseng core department The SEM image of the active carbon with a BET specific surface area of 2, ll3 m2/g is the second servant of the SEM image of the activated carbon, and the seventh figure (D) of the court is shown in the fifth figure (A), which is obtained from the core of the bagasse, the BET ratio. SEM image of activated carbon with a surface area of 3,120 m2/g. ^ Example 1) y.

第八圖(A)係為第五圖⑻中所示,由甘嚴渣外表 獲得BET比表面積為889m2/g之活性碳之SEM影像。。斤 施例1) 〜。(實 第八圖⑻係為第五圖⑻中所示’由甘蔗渣外表 獲得BET比表面積為!,682m2/g之活性碳之SEM影。斤 施例1) (實 第八圖(C)係為第五圖(B)中所示,由甘 獲得順比表面積為2,_m2/g之活性碳之、 施例1) (實 第八圖(D)係為第五圖⑻中所示,由甘嚴渣外表 獲得BET比表面積為3,328m2/g之活性碳之se ^ 施例1) 穴實 第九圖係為揭示由甘舰的芯部+外表皮部、 各(自實所施獲:^活性破,77K之的氛氣吸 第十圖係為揭示由甘嚴逢的The eighth diagram (A) is an SEM image of activated carbon having a BET specific surface area of 889 m 2 /g from the appearance of the slag residue as shown in the fifth diagram (8). . Jin Example 1) ~. (The eighth figure (8) is the SEM image of the activated carbon with a BET specific surface area of !, 682 m2/g from the appearance of the bagasse. The first example (C) is shown in the fifth figure (8). As shown in the fifth diagram (B), the activated carbon having a normal surface area of 2,_m2/g is obtained from Gan, and the first embodiment (D) is shown in the fifth figure (8). From the appearance of the slag residue, the seb with a BET specific surface area of 3,328 m2/g is obtained. Example 1) The ninth figure of the hole is revealed by the core of the Gan ship + the outer skin, each Obtained: ^ Active break, the tenth figure of the 77K atmosphere is revealed by Gan Yanfeng

:卜表皮部等各自所獲得之活性碳之BET比=與= 量之關係之圖表。(實施例i) 、電I 200932676 【主要元件符號說明】 1. 電雙層電容器 2. 分隔膜 3. 上侧分極性電極 4. 下側分極性電極 5. 上側集電極 6. 下侧集電極: A graph showing the relationship between the BET ratio of activated carbon obtained by each of the epidermis and the like and the amount of =. (Embodiment i), electric I 200932676 [Description of main component symbols] 1. Electric double layer capacitor 2. Separator diaphragm 3. Upper side polarity electrode 4. Lower side polarity electrode 5. Upper side collector 6. Lower side collector

7. 收納盒7. Storage box

22twenty two

Claims (1)

200932676 十、申請專利範圍: 1. 一種活性碳製造方法,其特徵為包含: 以從甘庶、/查獲得之原料進行碳化獲得碳·化物之 步驟;及 將前述碳化物以鹼活性化處理獲得活性碳之步 驟。 2. 如申請專利範圍第1項之活性碳製造方法,其中前述 原料係為經由使前述甘蔗渣芯部與外皮部分離後所 取得之外皮部份。 3. 如申請專利範圍第1項或第2項之活性碳製造方法, 其中前述以鹼活性化處理所獲得之BET比表面積係 為3000〜3500m2/g之範圍内。 4. 如申請專利範圍第1項、第2項或第3項之活性碳製 造方法,其中前述碳化時之碳化溫度係為673〜1,073K 之範圍内。 5. 如申請專利範圍第1項至第4項中任一項之活性碳製 造方法,其中前述用於鹼活性化之鹼係為鹼金屬氫氧 化物。 6. 如申請專利範圍第1項至第5項中任一項之活性碳製 造方法,其中於前述鹼活性化時,鹼比前述碳化物之 重量比係為4〜9之範圍。 7. 如申請專利範圍第1項至第6項中任一項之活性碳製 造方法,其中前述鹼活性化的活化溫度係為 823Κ~1,323Κ之範圍内。 8. 如申請專利範圍第1項至第7項中任一項之活性碳製 23 200932676 造方法,其中前述鹼活性化之活性化溫度係為較前述 碳化時之碳化溫度高100K〜300K範圍之溫度。 9. 如申請專利範圍第1項至第8項中任一項之活性碳製 造方法,其中前述活性碳係為電雙層電容器用之活性 碳。 10. —種電雙層電容器之製造方法,該電雙層電容器係具 備一對分極性電極、與該對分極性電極間所配置之分 隔膜、與該對分極性電極各自接續的一對集電極、及 與該對分極性電極所接觸之電解質,其特徵為: 前述之一對分極性電極中最少有一極的主要成 份為活性碳;及 , 前述的活性碳係經過從甘蔗渣獲得之原料經碳 化獲得碳化物之步驟,及以將前述碳化物以鹼活性化 處理之步驟獲得。 11. 如申請專利範圍第10項之電雙層電容器之製造方 法,其中前述原料係為經由使前述甘嚴造芯部與外皮 Φ 部分離後所取得之外皮部份。 12. 如申請專利範圍第10項或第11項所述之電雙層電容 器之製造方法,其中前述活性碳之電雙層電容量係為 170〜195F/g之範圍内。 13. 如申請專利範圍第10項、第11項或第12項所述之 電雙層電容器之製造方法,其中前述用於鹼活性化之 驗係為驗金屬氳氧化物。 24200932676 X. Patent application scope: 1. A method for producing activated carbon, which comprises the steps of: carbonizing a raw material obtained by carbonization from a raw material obtained from kansui or/or inspecting; and obtaining the foregoing carbide by alkali activation treatment The step of activated carbon. 2. The method for producing activated carbon according to claim 1, wherein the raw material is a skin portion obtained by separating the core of the bagasse from the outer skin portion. 3. The method for producing activated carbon according to claim 1 or 2, wherein the BET specific surface area obtained by the alkali activation treatment is in the range of 3,000 to 3,500 m 2 /g. 4. The activated carbon production method according to the first, second or third aspect of the patent application, wherein the carbonization temperature in the carbonization is in the range of 673 to 1,073 K. 5. The activated carbon production method according to any one of claims 1 to 4, wherein the base for alkali activation is an alkali metal hydroxide. 6. The activated carbon production method according to any one of claims 1 to 5, wherein, in the activation of the base, the weight ratio of the base to the carbide is in the range of 4 to 9. 7. The activated carbon production method according to any one of claims 1 to 6, wherein the activation temperature of the alkali activation is in the range of 823 Κ to 1,323 Å. 8. The method for producing activated carbon according to any one of claims 1 to 7, wherein the activation temperature of the alkali activation is higher than the carbonization temperature of the carbonization in the range of 100 K to 300 K. temperature. 9. The activated carbon production method according to any one of claims 1 to 8, wherein the activated carbon is activated carbon for an electric double layer capacitor. 10. A method of manufacturing an electric double layer capacitor comprising: a pair of polarization electrodes; a separator film disposed between the pair of polar electrodes; and a pair of episodes connected to the pair of polar electrodes The electrode and the electrolyte in contact with the opposite polarity electrode are characterized in that: at least one of the polar electrodes has a main component of activated carbon; and the activated carbon is obtained from the bagasse The step of obtaining a carbide by carbonization, and the step of treating the above-mentioned carbide with an alkali activation treatment. 11. The method of producing an electric double layer capacitor according to claim 10, wherein the raw material is a skin portion obtained by separating the sturdy core portion from the outer portion Φ portion. 12. The method of manufacturing an electric double layer capacitor according to claim 10, wherein the electric double layer capacitance of the activated carbon is in the range of 170 to 195 F/g. 13. The method for producing an electric double layer capacitor according to claim 10, wherein the alkali activation catalyst is a metal oxide. twenty four
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101757892B (en) * 2010-01-02 2012-07-04 桂林理工大学 Preparation method of bagasse active carbon/ferric oxide
TWI658484B (en) * 2014-03-28 2019-05-01 美商古柏科技公司 Electrochemical energy storage device with flexible metal contact current collector and methods of manufacture

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101757892B (en) * 2010-01-02 2012-07-04 桂林理工大学 Preparation method of bagasse active carbon/ferric oxide
TWI658484B (en) * 2014-03-28 2019-05-01 美商古柏科技公司 Electrochemical energy storage device with flexible metal contact current collector and methods of manufacture

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