JPH0610979B2 - Method for producing activated carbon for polarizable electrodes - Google Patents
Method for producing activated carbon for polarizable electrodesInfo
- Publication number
- JPH0610979B2 JPH0610979B2 JP60147518A JP14751885A JPH0610979B2 JP H0610979 B2 JPH0610979 B2 JP H0610979B2 JP 60147518 A JP60147518 A JP 60147518A JP 14751885 A JP14751885 A JP 14751885A JP H0610979 B2 JPH0610979 B2 JP H0610979B2
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- furnace
- long filament
- opening
- fibers
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/96—Carbon-based electrodes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/354—After-treatment
- C01B32/382—Making shaped products, e.g. fibres, spheres, membranes or foam
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/13—Energy storage using capacitors
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Inert Electrodes (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Carbon And Carbon Compounds (AREA)
- Inorganic Fibers (AREA)
- Electric Double-Layer Capacitors Or The Like (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は電気二重層キャパシタ、電池などに用いる分極
性電極のための繊維状活性炭の製造法に関する。TECHNICAL FIELD The present invention relates to a method for producing fibrous activated carbon for polarizable electrodes used in electric double layer capacitors, batteries and the like.
従来の技術 活性炭繊維を分極性電極として用いたキャパシタや電池
は既に知られている。活性炭電極の表面では、キャパシ
タ、電池いずれの場合も正,負イオンの吸脱着による電
気二重層の形成反応が主に起きており、この部分での荷
電の蓄積が一方の電極反応となる。2. Description of the Related Art Capacitors and batteries using activated carbon fibers as polarizable electrodes are already known. On the surface of the activated carbon electrode, the formation reaction of the electric double layer due to the adsorption and desorption of positive and negative ions mainly occurs in both the capacitor and the battery, and the accumulation of the charge in this portion becomes one electrode reaction.
ところで、このような活性炭繊維をその構成材料とする
分極性電極としては、従来、原料繊維を布状に織ってこ
れをそのまま炭化賦活し、活性炭繊維布としてそのまま
分極性電極に用いる構成と、ロングフィラメント状の繊
維を炭化賦活してこれを切断し、適当なバインダと混合
して抄紙して紙状、フェルト状の分極性電極として用い
る構成との2つが主流である。この2つの構成のうち、
活性炭繊維布を用いるものは、布のまま電極として用い
ることが可能なために製造が非常に容易である。これに
対し、ロングフィラメント状の繊維を出発原料とする、
紙、フェルト状分極性電極を用いるものは、原料繊維の
炭化賦活、切断、抄紙などのいくつかの工程を経てつく
られ、杆を用いるものよりも若干製造が繁雑になるが、
例えば紙を加圧などにより高密度にすることにより容積
あたりの活性炭充填量を大きくすることが可能である。By the way, as a polarizable electrode using such an activated carbon fiber as its constituent material, conventionally, a raw material fiber is woven into a cloth shape and carbonized and activated as it is, and the activated carbon fiber cloth is used as it is as a polarizable electrode. Mainly used is a configuration in which filamentary fibers are activated by carbonization, which are cut, mixed with an appropriate binder and made into paper to be used as a paper-like or felt-like polarizable electrode. Of these two configurations,
The one using activated carbon fiber cloth is very easy to manufacture because it can be used as an electrode as it is. On the other hand, using long filament fibers as a starting material,
Paper and those using felt-like polarizable electrodes are made through several processes such as carbonization activation of raw material fibers, cutting, and papermaking, and the production is slightly more complicated than that using rods,
For example, it is possible to increase the amount of activated carbon filled per volume by increasing the density of the paper by pressurizing.
従来、前記のロングフィラメント状の繊維の炭化賦活
は、第3図に示すようなバッチ式の炉を用いて行なわれ
ていた。すなわち、炉室部20、加熱部21、断熱部2
2、制御部23とからなる炉に、ロングフィラメント状
の繊維24を置き、これに賦活ガス供給装置25から賦
活ガスを作用させる方法である。Conventionally, the carbonization activation of the long filament fibers has been carried out using a batch type furnace as shown in FIG. That is, the furnace chamber portion 20, the heating portion 21, the heat insulating portion 2
2. A method in which long filament fibers 24 are placed in a furnace composed of a control unit 23 and activated gas from an activated gas supply device 25 is caused to act on the long filament fibers 24.
発明が解決しようとする問題点 ところが、上記のようなバッチ方式で炭化賦活を行なう
と、炉の昇温、降温に時間を要し、これに伴うエネルギ
も大きなものになり、生産性、コストの点で不利になっ
てしまう。また得られた活性炭繊維の特性(比表面積、
細孔分布)や、これを分極性電極の構成要素として用い
た電気二重層キャパシタの特性の点からも改善の余地が
ある。すなわち、(1)賦活ガスと被賦活繊維との接触反
応機会をより多くする、(2)炭化賦活時に発生する原料
繊維の分解ガスをできるだけ速かに系外に除去する、こ
とにより高比表面積の活性炭繊維を得ることができる。The problem to be solved by the invention is that when the carbonization activation is carried out by the batch method as described above, it takes time to raise and lower the temperature of the furnace, and the energy associated therewith also becomes large, resulting in high productivity and cost. You will be at a disadvantage. The characteristics of the obtained activated carbon fiber (specific surface area,
There is room for improvement in terms of the pore size distribution) and the characteristics of the electric double layer capacitor using this as a component of the polarizable electrode. That is, (1) increase the chances of contact reaction between the activated gas and the activated fiber, (2) remove the decomposition gas of the raw material fiber generated during carbonization activation to the outside of the system as quickly as possible, thereby increasing the high specific surface area. It is possible to obtain the activated carbon fiber of
本発明は、このようなロングフィラメント状の原料繊維
を出発物質として、特に高容量の分極性電極を与える活
性炭繊維を得る方法を提供するものである。The present invention provides a method for obtaining an activated carbon fiber which provides a polarizable electrode having a particularly high capacity, using such a long filament raw material fiber as a starting material.
問題点を解決するための手段 本発明は、上部および下部に開口部を有し、少なくとも
炉室下部の前記とは別の開口部から賦活ガスを供給し、
炉内を雰囲気制御可能にした炉の上部の開口部から下部
の開口部へ、または下部の開口部から上部の開口部へ、
ロングフィラメント状繊維からなるロービングまたはト
ウ状の物質を連続的に移動させてロングフィラメント状
繊維を活性炭化することを特徴とする。Means for Solving the Problems The present invention has openings in an upper part and a lower part, and supplies an activating gas from at least an opening different from the above in a lower part of a furnace chamber,
From the upper opening to the lower opening of the furnace that made the atmosphere inside the furnace controllable, or from the lower opening to the upper opening,
The present invention is characterized in that a roving or tow-shaped substance made of long filament-like fibers is continuously moved to activate and carbonize the long filament-like fibers.
作用 本発明によれば、高比表面積で、有効な細孔分布を有す
るロングフィラメント状の活性炭繊維が連続的に得られ
る。従って、これをチョップ状にして高密度な紙状にす
ることにより、活性炭布よりも高容量で小型の分極性電
極が得られる。Effects According to the present invention, long filament-like activated carbon fibers having a high specific surface area and an effective pore distribution are continuously obtained. Therefore, by chopping it into a high-density paper, a polarizable electrode having a higher capacity and a smaller size than the activated carbon cloth can be obtained.
特に布を原料にする場合と比べ、ロングフィラメント繊
維のロービング状、トウ状のものは、原料繊維の1本1
本が低密度に束ねられており、繊維を紡糸し、これを強
く織った織布に比べて、賦活ガスと被賦活繊維との接触
機会が多く、さらに炭化分解発生ガスも本発明の連続炉
では速やかに系外に除かれる。このために高容量の活性
炭繊維を得ることができる。Compared with the case where cloth is used as a raw material, long filament fiber roving-like or tow-like one is one raw material fiber.
Compared to a woven fabric in which books are bundled at a low density and fibers are spun and strongly woven, there are many opportunities for contact between the activated gas and the activated fibers, and the carbonization decomposition generated gas is also a continuous furnace of the present invention. Then it is promptly removed from the system. Therefore, a high capacity activated carbon fiber can be obtained.
実施例 第1図は実施例に用いた電気炉の構成を示す。1は炉室
本体であり、上部開口部2、下部開口部3を有する。4
は本体を加熱するためのヒータ、5は断熱層である。6
は下部開口部3と連通した収納箱、7は供給口8から本
体1内へ賦活ガスを供給する賦活ガス発生装置、9は原
料繊維である。Example FIG. 1 shows the configuration of the electric furnace used in the example. Reference numeral 1 denotes a furnace chamber body, which has an upper opening 2 and a lower opening 3. Four
Is a heater for heating the main body, and 5 is a heat insulating layer. 6
Is a storage box communicating with the lower opening 3, 7 is an activating gas generator that supplies activating gas from the supply port 8 into the main body 1, and 9 is a raw material fiber.
炉の上部開口部2から原料繊維9を投入し、賦活ガス発
生装置7からの水蒸気を窒素をキャリアガスとして賦活
ガス供給口8から炉室本体1に導びき、原料繊維の連続
的な炭化賦活を行なう。活性炭化したロングフィラメン
ト繊維10は下部収納箱6に得られる。連続賦活時の水
蒸気供給は1gのロングフィラメント状繊維に対して水
換算で4〜8ccに相当する量である。The raw material fiber 9 is charged from the upper opening 2 of the furnace, and the steam from the activation gas generator 7 is introduced from the activation gas supply port 8 to the furnace chamber body 1 by using nitrogen as a carrier gas to continuously activate the raw material fiber. Do. The activated carbonized long filament fiber 10 is obtained in the lower storage box 6. The steam supply during continuous activation is an amount corresponding to 4 to 8 cc in terms of water with respect to 1 g of long filament fiber.
次に、本発明の具体的な実施例について述べる。Next, specific examples of the present invention will be described.
実施例1 フェノール樹脂繊維のロングフィラメント(直径20μ
m)をたばねたロービング状の原料繊維を、第1図に示
す電気炉を用いて炭化賦活した。得られた活性炭繊維を
長さ1〜3mmのチョップ状に切断し、同じく長さ1〜3
mmの天然パルプと重量比60:40の割合で湿式混合
し、抄紙して乾燥した。得られた紙の坪量は100g/
m2、厚さは200μmである。この活性炭紙の片面にプ
ラズマ溶射法によってアルミニウムの集電体層を形成
し、これを直径10mmの円形に打ち抜いた。こうして得
た一対の分極性電極をセパレータを介して対向させて第
2図のような扁平形の電気二重層キャパシタを構成し
た。Example 1 Long filament of phenolic resin fiber (diameter 20 μ
The raw material fibers in the form of rovings that had a spring m) were activated by carbonization using the electric furnace shown in FIG. Cut the resulting activated carbon fiber into chopped pieces with a length of 1 to 3 mm, and
It was wet-mixed with a natural pulp of mm in a weight ratio of 60:40, paper-made and dried. The basis weight of the obtained paper is 100 g /
m 2 and thickness are 200 μm. An aluminum current collector layer was formed on one surface of the activated carbon paper by a plasma spraying method, and the aluminum current collector layer was punched into a circle having a diameter of 10 mm. The pair of polarizable electrodes thus obtained were opposed to each other with a separator interposed therebetween to form a flat electric double layer capacitor as shown in FIG.
第2図において11,12は分極性電極、13,14は
それらの集電体層、15はセパレータ、16はガスケッ
トリング、17は金属ケース、18は金属蓋である。な
お、電解液にはプロピレンカーボネートにテトラエチル
アンモニウムパークロレートを30重量%溶解した溶液
を用いた。In FIG. 2, 11 and 12 are polarizable electrodes, 13 and 14 are collector layers thereof, 15 is a separator, 16 is a gasket ring, 17 is a metal case, and 18 is a metal lid. As the electrolytic solution, a solution prepared by dissolving 30% by weight of tetraethylammonium perchlorate in propylene carbonate was used.
実施例2 実施例の活性炭繊維と天然パルプとを重量比60:40
の割合で混合し、坪量150g/m2に抄紙後、加圧カレ
ンダーロール加工をして厚さを200μmとした。この
活性炭紙を用いて、実施例1と同じ様にしてキャパシタ
を試作した。Example 2 A weight ratio of the activated carbon fiber of the example and the natural pulp is 60:40.
Were mixed at a ratio of 100 g / m 2 to produce a paper having a basis weight of 150 g / m 2 , and then pressure calendered to a thickness of 200 μm. Using this activated carbon paper, a capacitor was prototyped in the same manner as in Example 1.
実施例3 実施例1と同じ方法でロングフィラメント状活性炭繊維
をつくり、これを長さ1〜3cmに切断し相互にからめ合
わせて坪量100g/m2、厚さ250μmのフェルトと
し、その片面にアルミニウム集電体層をプラズマ溶射法
によって形成し、以下実施例1と同じ方法でキャパシタ
を試作した。Example 3 A long filament-like activated carbon fiber was prepared in the same manner as in Example 1, cut into lengths of 1 to 3 cm and interlocked with each other to give a felt having a basis weight of 100 g / m 2 and a thickness of 250 μm, and one side thereof. An aluminum current collector layer was formed by plasma spraying, and a capacitor was produced as a trial by the same method as in Example 1 below.
実施例4 実施例1で得た活性炭紙の片面にアルミニウム層をプラ
ズマ溶射法により形成し、これを3cm×5cmの大きさに
切断した。この電極2枚をそれらの活性炭紙側をセパレ
ータを介して対向させるとともに、アルミニウム層に沿
って厚さ0.02mmのアルミニウム箔を配して渦巻状に捲回
して円筒形のキャパシタを構成した。電解液は実施例1
と同じである。Example 4 An aluminum layer was formed on one surface of the activated carbon paper obtained in Example 1 by a plasma spraying method and cut into a size of 3 cm × 5 cm. These two electrodes were made to face each other with their activated carbon paper sides via a separator, and an aluminum foil having a thickness of 0.02 mm was arranged along the aluminum layer and spirally wound to form a cylindrical capacitor. The electrolytic solution is Example 1
Is the same as.
実施例5 実施例1で得られた活性炭紙の片面にアルミニウム層を
プラズマ溶射法により形成し、これを直径10mmの円形
に打抜いた。この分極性電極を正極にし、負極として、
リチウムをドープしたSn-Pb合金を用いて第2図のよう
な構造の電気化学装置を組み立てた。なお、電解液はプ
ロピレンカーボネートにリチウムパークロレートを溶解
したものを用いた。Example 5 An aluminum layer was formed on one surface of the activated carbon paper obtained in Example 1 by a plasma spraying method, and this was punched into a circle having a diameter of 10 mm. This polarizable electrode is used as a positive electrode and as a negative electrode,
An electrochemical device having a structure as shown in FIG. 2 was assembled using a Sn-Pb alloy doped with lithium. The electrolyte used was a solution of lithium perchlorate in propylene carbonate.
実施例6 実施例4の正極をそのままの材料で、負極には活性炭紙
の替わりに実施例5で用いたリチウムをドープしたSn-P
b合金箔を用い渦巻状に捲回して組み立てた。電解液は
実施例5と同じものを用いた。Example 6 Sn—P doped with lithium as used in Example 5 instead of activated carbon paper for the negative electrode using the same material as the positive electrode of Example 4
It was assembled by winding in a spiral shape using b alloy foil. The same electrolytic solution as in Example 5 was used.
比較例1 バッチ式炉で得られた活性炭繊維を用いて、実施例1と
同じようなキャパシタを試作した。Comparative Example 1 A capacitor similar to that of Example 1 was experimentally manufactured using the activated carbon fiber obtained in the batch furnace.
比較例2 活性炭繊維布をチョップ状にして実施例1と同じような
キャパシタを試作した。Comparative Example 2 An activated carbon fiber cloth was chopped to manufacture a capacitor similar to that of Example 1.
比較例3 目付100g/m2の活性炭繊維布を直径10mmの円形に
打ち抜いた分極性電極を用いて第1図のようなキャパシ
タを試作した。Comparative Example 3 A capacitor as shown in FIG. 1 was manufactured using a polarizable electrode obtained by punching an activated carbon fiber cloth having a basis weight of 100 g / m 2 into a circular shape having a diameter of 10 mm.
上記のキャパシタの特性として、25℃における容量C
25、−25℃における容量をC-25としたときの1−C
-25/C25及び1KHzにおけるインピーダンスを次表に示
す。As a characteristic of the above capacitor, the capacitance C at 25 ° C.
25 , 1-C when the capacity at -25 ° C is C- 25
The impedance at -25 / C 25 and 1KHz shown in the following table.
発明の効果 以上のように、本発明によれば、ロングフィラメント状
の繊維から連続的に、高容量の分極性電極を与える活性
炭繊維を得ることができる。 EFFECTS OF THE INVENTION As described above, according to the present invention, it is possible to continuously obtain activated carbon fibers that provide a high-capacity polarizable electrode from long filament fibers.
第1図は本発明の実施例に用いた炉の縦断面略図、第2
図はキャパシタの一例を示す縦断面図、第3図は従来の
炉の縦断面略図である。 1……炉室本体、2,3……開口部、4……ヒータ、6
……収納室、8……ガス供給口。FIG. 1 is a schematic vertical sectional view of a furnace used in an embodiment of the present invention,
FIG. 1 is a vertical sectional view showing an example of a capacitor, and FIG. 3 is a schematic vertical sectional view of a conventional furnace. 1 ... furnace chamber main body, 2, 3 ... opening, 4 ... heater, 6
…… Storing room, 8 …… Gas supply port.
フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 H01M 4/04 Z (72)発明者 棚橋 一郎 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (56)参考文献 特開 昭53−31820(JP,A) 特開 昭51−121739(JP,A) 特開 昭60−25166(JP,A) 特開 昭60−28170(JP,A) 特公 昭54−1815(JP,B2) 特公 昭53−47420(JP,B2)Continuation of the front page (51) Int.Cl. 5 Identification number In-house reference number FI Technology display location H01M 4/04 Z (72) Inventor Ichiro Tanahashi 1006 Kadoma, Kadoma-shi, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56 ) Reference JP 53-31820 (JP, A) JP 51-121739 (JP, A) JP 60-25166 (JP, A) JP 60-28170 (JP, A) JP 54-1815 (JP, B2) Japanese Patent Publication Sho 53-47420 (JP, B2)
Claims (1)
部と連通した収納箱とを有し、少なくとも炉室下部の別
の開口部から、1gのロングフィラメント状繊維に対し
て水換算で4〜6ccの水蒸気ガスを供給し、炉内を雰囲
気制御可能にした炉の上部の開口部から下部の開口部
へ、または、下部の開口部から上部の開口部へ、ロング
フィラメント状繊維からなるロービングまたはトウ状の
物質を連続的に移動させて、前記ロングフィラメント状
繊維を活性炭化することを特徴とする分極性電極用活性
炭の製造法。Claims: 1. An upper opening and a lower opening, and a storage box communicating with the lower opening, and from at least another opening at the lower part of the furnace chamber, 4 g in terms of water for 1 g of long filament fiber. Roving made of long filament fiber from the upper opening to the lower opening or from the lower opening to the upper opening of the furnace that can supply the steam gas of ~ 6cc to control the atmosphere inside the furnace. Alternatively, a method for producing activated carbon for a polarizable electrode, which comprises continuously moving a tow-shaped substance to activate carbonize the long filament fibers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60147518A JPH0610979B2 (en) | 1985-07-04 | 1985-07-04 | Method for producing activated carbon for polarizable electrodes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60147518A JPH0610979B2 (en) | 1985-07-04 | 1985-07-04 | Method for producing activated carbon for polarizable electrodes |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS628448A JPS628448A (en) | 1987-01-16 |
| JPH0610979B2 true JPH0610979B2 (en) | 1994-02-09 |
Family
ID=15432143
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60147518A Expired - Lifetime JPH0610979B2 (en) | 1985-07-04 | 1985-07-04 | Method for producing activated carbon for polarizable electrodes |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0610979B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5170809B2 (en) | 2007-08-27 | 2013-03-27 | 山下ゴム株式会社 | Liquid seal vibration isolator |
| EP3021389B1 (en) | 2008-11-18 | 2018-07-11 | Johnson Controls Technology Company | Electrical power storage devices |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS51121739A (en) * | 1975-04-18 | 1976-10-25 | Otani Sugio | Carbon fiber aqueous solution type secondary battery |
| JPS5825043B2 (en) * | 1976-09-03 | 1983-05-25 | 東邦ベスロン株式会社 | Continuous production method of fibrous activated carbon |
-
1985
- 1985-07-04 JP JP60147518A patent/JPH0610979B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS628448A (en) | 1987-01-16 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |