JP2986830B2 - Engine exhaust gas treatment device - Google Patents
Engine exhaust gas treatment deviceInfo
- Publication number
- JP2986830B2 JP2986830B2 JP2052411A JP5241190A JP2986830B2 JP 2986830 B2 JP2986830 B2 JP 2986830B2 JP 2052411 A JP2052411 A JP 2052411A JP 5241190 A JP5241190 A JP 5241190A JP 2986830 B2 JP2986830 B2 JP 2986830B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- magnetite
- hydrogen
- gas treatment
- engine
- 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 - Fee Related
Links
- 239000007789 gas Substances 0.000 claims description 50
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 40
- 239000001257 hydrogen Substances 0.000 claims description 28
- 229910052739 hydrogen Inorganic materials 0.000 claims description 28
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 18
- 229910052760 oxygen Inorganic materials 0.000 description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 19
- 239000001301 oxygen Substances 0.000 description 19
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 16
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 16
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 15
- 230000002950 deficient Effects 0.000 description 11
- 150000002431 hydrogen Chemical class 0.000 description 10
- 229910002092 carbon dioxide Inorganic materials 0.000 description 8
- 239000001569 carbon dioxide Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 235000000396 iron Nutrition 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- PXXKQOPKNFECSZ-UHFFFAOYSA-N platinum rhodium Chemical compound [Rh].[Pt] PXXKQOPKNFECSZ-UHFFFAOYSA-N 0.000 description 1
- ICTAZHZJEOVXOW-UHFFFAOYSA-N platinum vanadium Chemical compound [V].[Pt].[Pt].[Pt] ICTAZHZJEOVXOW-UHFFFAOYSA-N 0.000 description 1
- 238000011403 purification operation Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 229910000859 α-Fe Inorganic materials 0.000 description 1
Landscapes
- Catalysts (AREA)
- Exhaust Gas After Treatment (AREA)
- Treating Waste Gases (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) この発明は、ガソリンエンジンやヂーゼルエンジンの
排気ガスを浄化して炭酸ガスの排気を抑えたり、窒素酸
化物の排気を無くす排気ガスの処理装置に関する物であ
る。The present invention relates to an exhaust gas processing apparatus for purifying exhaust gas of a gasoline engine or a diesel engine to suppress the emission of carbon dioxide gas and to eliminate the emission of nitrogen oxides. It is about.
(従来技術) 従来、エンジンからの排気ガスを浄化する方法は多数
の研究者によって種々開発されてきたが、そのなかで
も、白金バナジュウムや白金ロジュウム等の複数の触媒
を排気ガス通路に直列的に並べて一酸化炭素を酸化して
炭酸ガスしたり、窒素酸化物NOxを窒素ガスN2にするも
のがあった。これは、特開昭63−113112号公報で代表さ
れる技術として既に公開されている。(Prior Art) Conventionally, various methods for purifying exhaust gas from an engine have been developed by many researchers. Among them, a plurality of catalysts such as platinum vanadium and platinum rhodium are serially connected to an exhaust gas passage. or carbon dioxide and alongside oxidizing carbon monoxide, nitrogen oxides NOx was something to nitrogen gas N 2. This is already disclosed as a technique represented by Japanese Patent Application Laid-Open No. 63-113112.
(発明が解決しようとする問題点) 従来装置は、コストが高くなると共に、一酸化炭素を
炭酸ガスとして排気させてしまい、現在世界中で温暖化
の要因になっている炭酸ガスの放出は抑えなければなら
ないにも拘らず、この従来装置は一酸化炭素を炭酸ガス
にして排出するために完全な浄化対策になっていない。(Problems to be Solved by the Invention) The conventional apparatus increases the cost and exhausts carbon monoxide as carbon dioxide, thereby suppressing the emission of carbon dioxide, which is currently causing global warming worldwide. In spite of having to do so, this conventional device does not provide a complete purification measure because carbon monoxide is converted into carbon dioxide gas and discharged.
更に、複数箇所の格別な触媒中を排気ガスは通過しな
ければならないために、エンジンの出力が低下してそれ
だけ多くの燃料が必要になりこのために更に多くの排気
ガスが発生して本質的な排気ガスの浄化にならないとい
う問題点があった。Further, since exhaust gas must pass through a plurality of special catalysts, the output of the engine is reduced, so that more fuel is required, and as a result, more exhaust gas is generated, and There is a problem that the exhaust gas cannot be purified.
(問題点を解決する手段) 前記の問題点を解決するために、この発明は基本的な
排気ガスの触媒としてマグネタイトを触媒として使用し
たことが特徴であり、つぎの各発明によって排気ガスの
浄化を行う。(Means for Solving the Problems) In order to solve the above problems, the present invention is characterized in that magnetite is used as a basic catalyst for exhaust gas as a catalyst. I do.
第1番目の発明は、250℃〜350℃付近に保温する恒温
部にマグネタイトが収納されてこのマグネタイトに気体
が接触して通過できる排気ガス処理部を複数個設け、エ
ンジンからの排気ガスと水素源あるいは水素発生装置か
らの水素とが切替弁で格別に送り込まれるように構成す
るとともに、所定の時間毎に排気ガスと水素との送込み
が逆になるよう構成してなるエンジンの排気ガス処理装
置である。In the first invention, magnetite is housed in a constant temperature section which keeps the temperature around 250 ° C. to 350 ° C., and a plurality of exhaust gas treatment sections through which gas can come in contact with and pass through the magnetite are provided. An exhaust gas treatment for an engine in which hydrogen from a source or a hydrogen generator is configured to be specially supplied by a switching valve, and configured so that the supply of exhaust gas and hydrogen is reversed at predetermined time intervals. Device.
第2番目の発明は、排気ガス通路の途中に概ね250℃
〜350℃近辺に保持する恒温部を設け、この恒温部にマ
グネタイトと排気ガスとが接触して通過する排気ガス処
理部を設け、このマグネタイト接触通路内に前記排気ガ
スと水素とを交互に送り込むよう構成し、その排気ガス
の送込み時間に対して水素側の送込み時間を短くしてな
るエンジンの排気ガス処理装置である。In the second invention, approximately 250 ° C.
A constant temperature section is maintained at about 350 ° C., and an exhaust gas processing section is provided in the constant temperature section through which magnetite and exhaust gas come in contact with each other, and the exhaust gas and hydrogen are alternately fed into the magnetite contact passage. An exhaust gas treatment device for an engine configured as described above, wherein the hydrogen-side supply time is shorter than the exhaust gas supply time.
(作用) 各発明の基本的な作用は、何れもマグネタイト(フェ
ライト)を有効に利用したものである。即ち、マグネタ
イトの分子構造は陽イオンを2個保有した2価の鉄(Fe
2★)1個と3個保有した3価の鉄(Fe3★)2個が存在
して計8価のプラス電荷になり、これが陰イオンを保有
する酸素(O2)4個と結び付いてFe3O4の安定したマグ
ネタイトになっているが、このマグネタイトを300℃近
辺のもとでは水素(H2)と反応して酸素(O2)が水(H2
O)になって逃げ、酸素が欠乏した活性のマグネタイト
が得られる。即ち、活性のマグネタイトは、以下、酸素
欠乏マグネタイト(Fe3O4−x)と呼ぶが、この活性化
されたマグネタイトは300℃の付近では酸素分子を要求
する科学反応可能な状態にある。(Function) The basic function of each invention is to effectively utilize magnetite (ferrite). That is, the molecular structure of magnetite is divalent iron (Fe) having two cations.
2 ★) One trivalent iron (Fe 3 ★) and two trivalent irons (Fe 3 ★) are present, resulting in a total of eight positive charges, which are combined with four oxygen (O 2 ) holding anions. Fe 3 O 4 is a stable magnetite, which reacts with hydrogen (H 2 ) at around 300 ° C. to convert oxygen (O 2 ) to water (H 2
O) escapes to give oxygen-deficient active magnetite. That is, the active magnetite is hereinafter referred to as oxygen-deficient magnetite (Fe 3 O 4 -x). At around 300 ° C., the activated magnetite is in a state capable of performing a scientific reaction requiring oxygen molecules.
したがって、この状態にした酸素欠陥マグネタイトに
炭酸ガスを反応させると炭素と不活性状態のマグネタイ
トになり、次に、水素をこの不活性マグネタイトに反応
させると急速に活性マグネタイトと水になる。これを科
学反応式にすると、 Fe3O4+yH2→Fe3O4_x+yH2O Fe3O4_x+1/2yCO2→1/2yC+Fe3O4 である。Therefore, when carbon dioxide gas is reacted with the oxygen-deficient magnetite in this state, the magnetite becomes inactive with carbon, and when hydrogen reacts with this inert magnetite, active magnetite and water are rapidly formed. If this is made into a scientific reaction formula, it is Fe 3 O 4 + yH 2 → Fe 3 O 4 _x + yH 2 O Fe 3 O 4 _x + 1 / 2yCO 2 → 1 / 2yC + Fe 3 O 4 .
基本的な発明の作用は上述の通りであるが、第1番目
の発明においては、排気ガスの浄化を連続状態で効率よ
く行なうために複数の浄化反応装置部分を設けて排気ガ
ス浄化中の装置と不活性になったマグネタイトを活性化
させる活性化中の装置を交互に切換えて一層の効率を図
る。The operation of the basic invention is as described above. However, in the first invention, a plurality of purification reaction device parts are provided to efficiently purify exhaust gas in a continuous state, and an apparatus for purifying exhaust gas is provided. Further, the efficiency of the apparatus being activated is alternately switched to activate the magnetite which has become inactive.
2番目の発明は、酸素欠陥マグネタイト排気ガス中の
酸素と結合して不活性なマグネタイトになった状態から
再度酸素欠陥マグネタイトにする場合にはマグネタイト
の表面近くのみを酸素欠陥マグネタイトにして急速な反
応を気体すれば足りるから、無駄な水素の補給をなく
し、排気ガスとの反応時間を少しでも長くして効率的な
排気ガスの浄化をさせる。In the second invention, when oxygen-deficient magnetite is combined with oxygen in exhaust gas to form an inactive magnetite from oxygen-deficient magnetite to oxygen-deficient magnetite again, only the vicinity of the surface of the magnetite is converted to oxygen-deficient magnetite to rapidly react. Since it is sufficient to gasify the exhaust gas, unnecessary supply of hydrogen is eliminated, and the reaction time with the exhaust gas is lengthened as much as possible, thereby purifying the exhaust gas efficiently.
(実施例) この発明の一実施例について詳述すると、1はエンジ
ンで、2がその排気通路である。3は水素発生装置で、
第1図で開示したものは水の電気分解で水素を発生する
構成になっている。4は水素の取出し通路である。5は
切換弁で、これは二つの流路のものを互いに入れ替えて
流せる2方向選択型の弁になっている。6は開閉弁であ
る。7,8は前記切換弁5の二つの出口側ポートに通ずる
流路9,10に格別に設けた排気ガス処理部であって、各流
路9,10の先端に着脱自在に連結した排気筒11,12の入口
部分にマグネタイト13を通気可能に充填したセル14を内
装させ、更に、セル14が内装される排気筒11,12の外周
部にヒータ15を設けてマグネタイト13が内装された部分
を300℃近辺の温度に保つように構成している。尚、こ
のヒータ15はエンジン熱で300℃に保つ場合は必要でな
い。Embodiment An embodiment of the present invention will be described in detail. Reference numeral 1 denotes an engine, and reference numeral 2 denotes an exhaust passage. 3 is a hydrogen generator,
The structure disclosed in FIG. 1 is configured to generate hydrogen by electrolysis of water. Reference numeral 4 denotes a hydrogen extraction passage. Reference numeral 5 denotes a switching valve, which is a two-way selection type valve which can exchange two flow passages with each other. Reference numeral 6 denotes an on-off valve. Reference numerals 7 and 8 denote exhaust gas treatment units provided in flow paths 9 and 10 communicating with the two outlet ports of the switching valve 5, respectively, and exhaust pipes detachably connected to tips of the flow paths 9 and 10. A cell 14 filled with magnetite 13 in a ventilated manner at the inlet portion of 11, 12 is further provided, and a heater 15 is provided on an outer peripheral portion of exhaust pipes 11 and 12 in which the cell 14 is provided, and the magnetite 13 is provided therein. Is maintained at a temperature around 300 ° C. This heater 15 is not necessary when the temperature is maintained at 300 ° C. by the engine heat.
上例の作用について詳述すると、第1図では、エンジ
ン1から排出される炭酸ガスCO2,窒素酸化物NOxの混合
した排気ガスが切換弁5を経て流路9に流れ、一方水素
発生装置3で造られた水素H2が流路4及び開閉弁6を通
って切換弁5を経て流路10に流れる。すると、排気ガス
の流れる流路9に接続された排気ガス処理部7では、マ
グネタイト13が予め水素H2を通して活性にしておけばマ
グネタイト自体が酸素欠陥マグネタイトFe3O4_xに変身
しているから、炭酸ガスCO2の酸素O2あるいはNOxの酸素
Oxを該酸素欠陥マグネタイトが取り込み、炭素Cが析出
したり、あるいは窒素ガスN2になって飛び出る。The operation of the above example will be described in detail. In FIG. 1, the exhaust gas mixed with carbon dioxide CO 2 and nitrogen oxide NOx discharged from the engine 1 flows through the switching valve 5 to the flow path 9 while the hydrogen generator The hydrogen H 2 produced in 3 flows through the flow path 4 and the on-off valve 6 to the flow path 10 via the switching valve 5. Then, in the exhaust gas processing section 7 connected to the flow path 9 through which the exhaust gas flows, if the magnetite 13 is activated through hydrogen H 2 in advance, the magnetite itself is transformed into oxygen-deficient magnetite Fe 3 O 4 _x. , carbon dioxide CO 2 oxygen O 2 or oxygen NOx
Ox is taken in by the oxygen-deficient magnetite, and carbon C is deposited or jumps out as nitrogen gas N 2 .
一方、水素H2が送り込まれる排気ガス処理部8では、
不活性になっているマグネタイトFe3O4に水素H2が働
き、この水素H2がマグネタイト中の酸素O2を追い出して
酸素欠陥マグネタイトになる。On the other hand, in the exhaust gas processing unit 8 into which the hydrogen H 2 is sent,
Hydrogen H 2 acts on the inactivated magnetite Fe 3 O 4 , and this hydrogen H 2 drives out oxygen O 2 in the magnetite to become oxygen-deficient magnetite.
即ち、排気ガス処理部8側では、 Fe3O4+H2→Fe3O4_x+xH2O あるいは、 Fe3O4_x+2NOx→N2+Fe3O4 の化学反応を起こして浄化される。That is, on the exhaust gas processing unit 8 side, purification is performed by causing a chemical reaction of Fe 3 O 4 + H 2 → Fe 3 O 4 —x + xH 2 O or Fe 3 O 4 —x + 2NOx → N 2 + Fe 3 O 4 .
尚、窒素酸化物NOxについては、極めて速い反応にな
り、窒素酸化物の浄化は相早く行なわれるが、炭酸ガス
CO2については、反応が遅く、排気ガス処理部を加圧状
態にすることが望ましい。It should be noted that nitrogen oxide NOx reacts very quickly, and purification of nitrogen oxides is performed promptly.
As for CO 2 , the reaction is slow, and it is desirable that the exhaust gas treatment section be pressurized.
そして、所定時間(1分〜3分程度が適当)第1図の
状態(線図で示すと第2図)を続けた後、今後は切換弁
5を第3図の通り切換えて排気ガスが流路10に、水素H2
が流路9に流れるように切換えると、前記と同じ作用で
排気ガスが浄化されることになる。After continuing the state of FIG. 1 for a predetermined time (approximately 1 to 3 minutes is appropriate) (FIG. 2 when shown in a diagram), the switching valve 5 is switched as shown in FIG. In the flow path 10, hydrogen H 2
Is switched to flow through the flow path 9, the exhaust gas is purified by the same operation as described above.
そして、水素H2が送込み側の開閉弁6は、前記切換弁
5の切換えに連動して所定時間(10秒〜30秒程度)開口
すると閉口するようにしておけば、水素H2の無駄をなく
すことができる。Then, the opening and closing valve 6 of hydrogen H 2 are side infeed is, if in conjunction with the switching of the switching valve 5 so as to closed to a predetermined time (10 seconds to 30 seconds) opening, waste of hydrogen H 2 Can be eliminated.
(発明の効果) 第1番目の発明によると、特定の排気ガス処理部で排
気ガスを浄化反応中に、浄化作用を終えた他の排気ガス
処理部のマグネタイトを活性化した酸素欠陥マグネタイ
トに還元でき、連続して排気ガス浄化を行なうことがで
き、浄化効率を向上できる。(Effects of the Invention) According to the first invention, during a purification reaction of an exhaust gas in a specific exhaust gas processing unit, magnetite of another exhaust gas processing unit that has completed the purification operation is reduced to an oxygen-deficient magnetite activated. The exhaust gas can be continuously purified, and the purification efficiency can be improved.
第2番目の発明によると、マグネタイトを酸素欠陥マ
グネタイトにかえる水素H2の使用量を減らすことができ
る。According to a second aspect of the invention, it is possible to reduce the amount of hydrogen H 2 to change the magnetite to oxygen defect magnetite.
図は、この発明の一実施例であって、第1図は要部の断
面図、第2図はその簡略図、第3図は要部の簡略図であ
る。 図中の記号 1はエンジン、2は排気通路、3は水素発生装置、4は
水素取出し通路、5は切換弁、6は開閉弁、7,8は排気
ガス処理部、9,10は流路、11,12は排気路を示す。FIG. 1 shows an embodiment of the present invention. FIG. 1 is a sectional view of a main part, FIG. 2 is a simplified view of the main part, and FIG. 3 is a simplified view of a main part. In the figure, 1 is an engine, 2 is an exhaust passage, 3 is a hydrogen generator, 4 is a hydrogen extraction passage, 5 is a switching valve, 6 is an on-off valve, 7, 8 is an exhaust gas processing section, and 9 and 10 are flow paths. , 11 and 12 indicate exhaust paths.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F01N 3/10 F01N 3/28 B01D 53/34 B01J 23/745 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 6 , DB name) F01N 3/10 F01N 3/28 B01D 53/34 B01J 23/745
Claims (2)
ネタイトが収納されてこのマグネタイトに気体が接触し
て通過できる排気ガス処理部を複数個設け、エンジンか
らの排気ガスと水素源あるいは水素発生装置からの水素
とが切替弁で各別に送り込まれるように構成するととも
に、所定時間毎に排気ガスと水素との送込みが逆になる
よう構成してなるエンジンの排気ガス処理装置。A magnetite is housed in a constant temperature section which keeps the temperature around 250 ° C. to 350 ° C., and a plurality of exhaust gas treatment sections are provided, through which gas can come into contact with and pass through the magnetite, and an exhaust gas from an engine and a hydrogen source or An exhaust gas treatment device for an engine, wherein hydrogen from a hydrogen generator is separately supplied by a switching valve, and the supply of exhaust gas and hydrogen is reversed at predetermined time intervals.
辺に保持される恒温部を設け、この恒温部にマグネタイ
トと排気ガスとが接触して通過する排気ガス処理部を設
け、このマグネタイト接触通路内に前記排気ガスと水素
とを交互に送り込むよう構成し、その排気ガスの送込み
時間に対して水素側の送込み時間を短くしてなるエンジ
ンの排気ガス処理装置。2. A constant temperature section which is maintained at about 250 ° C. to 350 ° C. in the middle of the exhaust gas passage, and an exhaust gas treatment section through which magnetite and exhaust gas come into contact with and pass through the constant temperature section. An exhaust gas treatment device for an engine, wherein the exhaust gas and the hydrogen are alternately fed into a magnetite contact passage, and the time for feeding on the hydrogen side is shortened with respect to the time for sending the exhaust gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2052411A JP2986830B2 (en) | 1990-03-02 | 1990-03-02 | Engine exhaust gas treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2052411A JP2986830B2 (en) | 1990-03-02 | 1990-03-02 | Engine exhaust gas treatment device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03253715A JPH03253715A (en) | 1991-11-12 |
| JP2986830B2 true JP2986830B2 (en) | 1999-12-06 |
Family
ID=12914045
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2052411A Expired - Fee Related JP2986830B2 (en) | 1990-03-02 | 1990-03-02 | Engine exhaust gas treatment device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2986830B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009172467A (en) * | 2008-01-22 | 2009-08-06 | Nippon Steel Corp | Metal carrier and catalyst for decomposition of carbon dioxide in gas, production method thereof, and method for decomposition of carbon dioxide |
-
1990
- 1990-03-02 JP JP2052411A patent/JP2986830B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03253715A (en) | 1991-11-12 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |