JPH06146852A - Diesel engine exhaust gas purifying device - Google Patents
Diesel engine exhaust gas purifying deviceInfo
- Publication number
- JPH06146852A JPH06146852A JP4350104A JP35010492A JPH06146852A JP H06146852 A JPH06146852 A JP H06146852A JP 4350104 A JP4350104 A JP 4350104A JP 35010492 A JP35010492 A JP 35010492A JP H06146852 A JPH06146852 A JP H06146852A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- upstream
- diesel engine
- ceramic filter
- wire
- 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.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/28—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a plasma reactor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B3/00—Engines characterised by air compression and subsequent fuel addition
- F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Exhaust Gas After Treatment (AREA)
- Processes For Solid Components From Exhaust (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、燃焼排気ガス、特に
デイーゼルエンジンからの排気ガス中に含まれるすすを
セラミックフィルターを用いて効率良く捕集すると同時
に、捕集されたすすを放電プラズマによって低温酸化し
ガス化する事により、該セラミックフィルターの目詰り
を防止し、すすで生ずるフィルターの圧力損失の増加を
防止し、かつ上記プラズマが生成するラジカルの作用で
該排気ガス中のNOxなどのガス状汚染物質も酸化ない
し還元して除去し、大気汚染を防止する装置に関するも
のである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention efficiently collects soot contained in combustion exhaust gas, particularly exhaust gas from a diesel engine using a ceramic filter, and at the same time collects soot at a low temperature by a discharge plasma. By oxidizing and gasifying, the clogging of the ceramic filter is prevented, the increase in pressure loss of the filter caused by soot is prevented, and the gas such as NOx in the exhaust gas due to the action of radicals generated by the plasma. The present invention also relates to a device for preventing air pollution by oxidizing and reducing pollutants as well.
【0002】[0002]
【従来の技術】従来セラミックフィルターを用いてデイ
ーゼルエンジンの排気ガス中のすすを捕集する場合、捕
集した煤によってフィルターが目詰りを起こし、その圧
力損失が短時間で著しく増加してエンジンの効率が低下
してしまう。2. Description of the Related Art Conventionally, when soot in exhaust gas of a diesel engine is collected using a ceramic filter, the collected soot causes the filter to be clogged, and the pressure loss of the filter is significantly increased in a short time. The efficiency will decrease.
【0003】そのためセラミックフィルターの上流側に
バーナーを置いたり、セラミックフィルター自体にヒー
ターを入れて、捕集したすすを燃焼によりガス化し、目
詰りを防止している。Therefore, a burner is placed on the upstream side of the ceramic filter, or a heater is placed in the ceramic filter itself so that the collected soot is gasified by combustion to prevent clogging.
【0004】しかしながら、この場合均一に燃焼させる
ことは困難で、はじめに燃焼した部分に通気抵抗減少に
より、より多くのガスが流入、供給酸素量が増大して燃
焼速度が増し、ますます多くのガスが流入することとな
る。その結果そこの部分で過剰な燃焼熱が発生して温度
の異常上昇が起こり、セラミックフィルターが損耗し、
その寿命を著しく短縮していた。However, in this case, it is difficult to combust evenly, and more gas is introduced into the first combusted portion due to the reduction in ventilation resistance, the amount of oxygen supplied is increased, the combustion speed is increased, and more and more gas is increased. Will flow in. As a result, excessive combustion heat is generated in that part, an abnormal rise in temperature occurs, the ceramic filter wears,
It had shortened its life significantly.
【0005】またデイーゼルエンジンの排気ガスのいま
ひとつの問題であるNOxの除去には触媒を用いる方法
が取られている。In addition, a method using a catalyst is used to remove NOx which is another problem of the exhaust gas of a diesel engine.
【0006】しかしながら、すすを含むデイーゼルエン
ジン排気に対する高効率かつ長寿命のNOx除去触媒は
未だ完成されておらず、その上上記すす捕集用セラミッ
クフィルターと触媒を2重に用いると排気側の圧力損失
はますます増加し、エンジン効率の低下は避けられなか
った。However, a highly efficient and long-life NOx removal catalyst for a diesel engine exhaust containing soot has not yet been completed, and when the above-mentioned ceramic filter for collecting soot and the catalyst are used in duplicate, the pressure on the exhaust side is increased. The losses are increasing and the loss of engine efficiency is inevitable.
【0007】[0007]
【発明が解決しようとする課題】この発明の目的は、す
す捕集用セラミックフィルターに捕集されたすすを均一
に且つ低温で酸化する事によりフィルターの過熱・損傷
なしにその目詰りを常に防止することである。SUMMARY OF THE INVENTION An object of the present invention is to prevent the clogging of a soot trapping ceramic filter without overheating or damage by uniformly oxidizing the soot trapped in the ceramic filter at a low temperature. It is to be.
【0008】また他の目的は、排気ガス中のガス状汚染
物質、特にNOxを同時に除去することである。Yet another object is to simultaneously remove gaseous pollutants, especially NOx, in the exhaust gas.
【0009】[0009]
【問題を解決するための手段】この発明のデイーゼルエ
ンジン排気ガス浄化装置は、デイーゼルエンジンの排気
ダクトに接続して、すすを含んだ排気ガスの入口と清浄
ガスの出口を有するケーシングを設け、その内部にガス
流を遮る如くにセラミックフィルターを設け、該セラミ
ックフィルターのフィルター要素を挟んで、ガスの流れ
を妨げない構造の少なくとも1つの電極要素からなるプ
ラズマ処理電極の2組を相互に絶縁のうえ配設し、この
両プラズマ処理電極に接続してその間に交流電圧を印加
するための交流電源を設け、該フィルター要素の少なく
とも1部を介して両プラズマ処理電極間に放電を発生さ
せるものである。DISCLOSURE OF THE INVENTION A diesel engine exhaust gas purifying apparatus of the present invention is provided with a casing connected to an exhaust duct of a diesel engine and having an inlet for exhaust gas containing soot and an outlet for clean gas. A ceramic filter is provided so as to block the gas flow inside, and two sets of plasma processing electrodes, each of which is composed of at least one electrode element having a structure that does not impede the gas flow, are mutually insulated by sandwiching the filter element of the ceramic filter. An AC power supply is provided to connect both plasma processing electrodes and to apply an AC voltage between them, and an electric discharge is generated between both plasma processing electrodes via at least a part of the filter element. .
【0010】この場合、上記の両プラズマ処理電極は上
記セラミックフィルターに近接して、その上流側と下流
側に金網ないし多孔板の電極要素を設けて構成するもの
である。In this case, both of the plasma treatment electrodes are constructed by providing wire mesh or perforated plate electrode elements on the upstream and downstream sides of the electrodes in the vicinity of the ceramic filter.
【0011】また必要に応じて、上記セラミックフィル
ターとして、ハニカム構造で多数の細長いガス通路群よ
り成ると共に該ガス通路の上流端と下流端が交互に閉塞
されて上流側に連通した上流側ガス通路群と下流側に連
通した下流側ガス通路群に分かれ、その隣合う両ガス通
路の間の隔壁が上記フィルター要素を構成するハニカム
型セラミックフィルターを用いると共に、上記2組のプ
ラズマ処理電極のうち、上流側電極は上記ハニカム型セ
ラミックフィルターの閉塞端の上流側にこれと近接して
設けられた金網ないし多孔板のいずれかの電極要素から
構成し、また下流側電極は上記ハニカム型セラミックフ
ィルターの該下流側ガス通路群に下流側から挿入された
針金状の電極要素から構成するものである。If desired, the ceramic filter is composed of a large number of elongated gas passages having a honeycomb structure, and the upstream and downstream ends of the gas passages are alternately closed to communicate with the upstream gas passages. And a group of downstream gas passages communicating with the downstream side, and a partition wall between the two adjacent gas passages uses a honeycomb ceramic filter in which the filter element constitutes the filter element. The upstream electrode is composed of any one of electrode elements of a wire mesh or a perforated plate which is provided close to the upstream side of the closed end of the honeycomb ceramic filter, and the downstream electrode is the honeycomb ceramic filter. It is composed of a wire-shaped electrode element inserted from the downstream side into the downstream gas passage group.
【0012】あるいは、この場合上記2組のプラズマ処
理電極のうち、上流側処理電極は上記ハニカム型セラミ
ックフィルターの上流側に針金状の電極要素を配設構成
してその下流側先端部が該上流側ガス通路群の入口付近
に位置する如くし、また下流側処理電極は該下流側ガス
通路群内に下流側から針金状の電極要素を挿入して構成
するものである。Alternatively, in this case, of the two sets of plasma processing electrodes, the upstream processing electrode is provided with a wire-shaped electrode element on the upstream side of the honeycomb type ceramic filter, and the downstream end portion thereof is the upstream side. The processing electrode is located near the inlet of the side gas passage group, and the downstream processing electrode is configured by inserting a wire-like electrode element from the downstream side into the downstream gas passage group.
【0013】この場合、必要に応じて上記上流側電極部
の針金状電極要素をそれぞれその先端が対向する該上流
側ガス通路の入口から該ガス通路内に挿入・抽出するた
めの挿入・抽出手段を設けるものである。In this case, inserting / extracting means for inserting / extracting the wire-like electrode elements of the upstream electrode section into the gas passages from the inlets of the upstream gas passages, the tips of which face each other, if necessary. Is provided.
【0014】あるいは必要に応じて上記2組のプラズマ
処理電極のうち、上流側処理電極は上記ハニカム型セラ
ミックフィルターの該上流側ガス通路群内にに上流側か
ら挿入された針金状の電極要素で構成し、また下流側処
理電極は該下流側ガス通路群内に下流側から挿入された
針金状の電極要素で構成するものである。Alternatively, if necessary, the upstream processing electrode of the two sets of plasma processing electrodes is a wire-like electrode element inserted from the upstream side into the upstream gas passage group of the honeycomb ceramic filter. Further, the downstream processing electrode is composed of a wire-shaped electrode element inserted from the downstream side into the downstream gas passage group.
【0015】あるいは必要に応じて上記2組のプラズマ
処理電極の双方を、該下流側ガス通路群内に下流側から
針金状の電極要素を挿入して構成し、かつその双方のプ
ラズマ処理電極に属する電極要素が互いに1つの上流側
ガス通路を介して対向する様にするものである。Alternatively, if necessary, both of the two sets of plasma processing electrodes are constructed by inserting wire-like electrode elements from the downstream side into the downstream side gas passage group, and both of the plasma processing electrodes are provided. The electrode elements to which they belong are opposed to each other via one upstream gas passage.
【0016】また上記の交流電源としては出力電圧の波
高値が3kV以上、出力周波数5kHz以上の高周波高
電圧を発生する高周波高圧電源を用いる物である。As the AC power supply, a high-frequency high-voltage power supply for generating a high-frequency high voltage having a peak value of output voltage of 3 kV or more and an output frequency of 5 kHz or more is used.
【0017】あるいは必要に応じて、上記の交流電源と
しては出力電圧波高値5kV以上、出力周波数50Hz
以上のパルス状高電圧を発生する高圧パルス電源を用い
るものである。If desired, the AC power supply may have an output voltage peak value of 5 kV or more and an output frequency of 50 Hz.
The high-voltage pulse power supply that generates the pulsed high voltage described above is used.
【0018】[0018]
【作用】上記2組のプラズマ処理電極の間に交流電圧を
連続的または間欠的に印加してセラミックフィルターの
すすが付着したフィルター要素を介して放電を発生させ
る。この放電のプラズマ化学作用で生成するラジカルに
よりすすを低温酸化することによりガス化して除去し、
すすによる上記フィルター要素の目詰りを防ぐ。これに
よって該セラミックフィルターの圧力損失を常に低く保
ち、デイーゼルエンジンの効率低下を防止する。An AC voltage is continuously or intermittently applied between the two sets of plasma treatment electrodes to generate a discharge through the soot-attached filter element of the ceramic filter. The radicals generated by the plasma chemistry of this discharge gasify and remove soot by low-temperature oxidation.
Prevents soot from clogging the filter element. This keeps the pressure loss of the ceramic filter low at all times and prevents the efficiency of the diesel engine from decreasing.
【0019】上記ラジカルの作用で、排気ガス中に含ま
れるNOx等のガス状汚染物質も同時に酸化または還元
して除去し、デイーゼルエンジンの排気ガスを浄化す
る。By the action of the radicals, gaseous pollutants such as NOx contained in the exhaust gas are simultaneously oxidized or reduced to be removed, and the exhaust gas of the diesel engine is purified.
【0020】[0020]
【実施例】図1はこの発明の基本概念を示す実施例1の
縦断面図を示す。デイーゼルエンジンの排気ダクト2に
介入してガス入口3およびガス出口4を接続したケーシ
ング5の内部にガス流を遮る如くにセラミックフィルタ
ー6を配設する。ただし、このセラミックフィルター6
は多孔質セラミックをフィルター要素とする板状、プリ
ーツ状、ハニカム状、円筒状等適当なあらゆる形状・構
造のセラミックフィルター一般を模式的に示したもので
ある。1 is a longitudinal sectional view of a first embodiment showing the basic concept of the present invention. A ceramic filter 6 is arranged inside the casing 5 which connects the gas inlet 3 and the gas outlet 4 by interposing the exhaust duct 2 of the diesel engine so as to block the gas flow. However, this ceramic filter 6
Is a schematic view of a ceramic filter generally having any suitable shape and structure such as plate, pleats, honeycomb, and cylinder having a porous ceramic as a filter element.
【0021】このセラミックフィルター6のフィルター
要素7の上流側と下流側にガスの通過を許す構造の電極
要素(例えば金網・金属製多孔板・金属製すだれ等)よ
りなる上流側プラズマ処理電極8と下流側プラズマ処理
電極9を設けて、その間に交流電源10より高周波高電
圧または高圧パルス電圧を連続的あるいは間欠的に印加
する。An upstream plasma processing electrode 8 comprising an electrode element (for example, a wire mesh, a metal perforated plate, a metal blind, etc.) having a structure that allows gas to pass through on the upstream side and the downstream side of the filter element 7 of the ceramic filter 6. A downstream plasma processing electrode 9 is provided, and a high frequency high voltage or a high voltage pulse voltage is continuously or intermittently applied from an AC power source 10 between them.
【0022】その結果両プラズマ処理電極8、9の間
に、上記フィルター要素7を誘電体として介在させた放
電が発生する。この放電は、該プラズマ処理電極8、9
と該フィルター要素7の表面との間のガス空間では無声
放電、また該フィルター要素7内部の空隙中ではボイド
放電の形態をとり、いずれも電子温度は極めて高いがイ
オン温度は低い低温プラズマ(非平衡プラズマともい
う)を生成し、酸化性および還元性の反応性に富むラジ
カルを豊富に作りだす。As a result, a discharge is generated between the two plasma processing electrodes 8 and 9 with the filter element 7 interposed as a dielectric. This discharge is caused by the plasma processing electrodes 8, 9
In the gas space between the filter element 7 and the surface of the filter element 7, there is a silent discharge, and in the void inside the filter element 7, there is a form of void discharge, both of which have a low electron temperature but a low ion temperature (low temperature plasma). (Also called equilibrium plasma) to produce abundant radicals rich in oxidizing and reducing reactivity.
【0023】このラジカルにより上記フィルター要素7
の上流側表面および内部空隙に付着したすすは低温酸化
されてCO2ないしCOとして排出され、その結果上記
セラミックフィルター6のフィルター要素7は常に清浄
に保たれ圧力損失を低く保つことが出来る。同時にこの
ラジカルによって排ガス中のNOxなどのガス状汚染物
質は酸化ないし還元され、除去される。This radical causes the filter element 7 to
The soot adhering to the upstream surface and the internal voids of CO 2 is oxidized at a low temperature and discharged as CO 2 or CO, so that the filter element 7 of the ceramic filter 6 can be kept clean and the pressure loss can be kept low. At the same time, the radicals oxidize or reduce gaseous pollutants such as NOx in the exhaust gas and remove them.
【0024】図2はすでに述べたハニカム型セラミック
フィルター11の斜視図、図3はこれを用いて本発明を
実施した実施例12の主要部の縦断面図である。このフ
ィルターはハニカム構造を有し、多孔質セラミック隔壁
13で隔てられた多数の細長いガス通路群14を有す
る。FIG. 2 is a perspective view of the above-mentioned honeycomb type ceramic filter 11, and FIG. 3 is a longitudinal sectional view of the main part of Embodiment 12 in which the present invention is carried out by using the same. This filter has a honeycomb structure and has a large number of elongated gas passage groups 14 separated by porous ceramic partition walls 13.
【0025】これらのガス通路群14はその上流端と下
流端において相隣る交互に上流側セラミック製閉塞部1
5と下流側セラミック製閉塞部16によって閉塞され、
上流側に連通し下流端が閉塞された上流側ガス通路群1
7と、下流側に連通し上流側が閉塞された下流側ガス通
路群18に分かれる。These gas passage groups 14 are adjacent to each other at the upstream end and the downstream end thereof, and are alternately adjacent to each other.
5 and the downstream ceramic blocking portion 16,
Upstream gas passage group 1 communicating with the upstream side and having a closed downstream end
7 and a downstream side gas passage group 18 communicating with the downstream side and closed on the upstream side.
【0026】そして排気ガスは該上流側ガス通路群17
内にその上流側開口部19から進入し、上記フィルター
要素7を構成する該多孔質セラミック隔壁13を通過し
て該下流側ガス通路群18内に入り、その下流側開口部
20から排出される。すすは該セラミック隔壁13の上
流側表面と、その内部空隙中に付着する。The exhaust gas is supplied to the upstream side gas passage group 17
Enters through the upstream opening 19, passes through the porous ceramic partition wall 13 constituting the filter element 7, enters the downstream gas passage group 18, and is discharged through the downstream opening 20. . The soot adheres to the upstream surface of the ceramic partition 13 and the internal voids.
【0027】8は上記上流側セラミック製閉塞部14の
上流側にこれと接近して設けられた金網21を電極要素
とする上流側プラズマ処理電極である。また9は上記下
流側ガス通路群18内にその下流側開口部20から奥ま
で挿入された針金22を電極要素とする下流側プラズマ
処理電極である。Reference numeral 8 is an upstream plasma processing electrode having a wire net 21 as an electrode element, which is provided on the upstream side of the upstream ceramic blocking portion 14 in close proximity thereto. Reference numeral 9 denotes a downstream plasma processing electrode having a wire 22 inserted into the downstream gas passage group 18 from the downstream opening 20 to the back as an electrode element.
【0028】いま両プラズマ処理電極8と9の間に交流
電源10より高周波高電圧または高圧パルス電圧を連続
的あるいは間欠的に印加すると、該針金電極要素22の
上流側先端部23と該金網電極要素22の間に誘電体で
ある上記上流側セラミック製閉塞部15および該セラミ
ック隔壁13の上流側開口部19近傍部分を介在して無
声放電が発生、これにより生成したラジカルが該上流側
開口部19から各上流側ガス通路群17内に進入し、該
セラミック隔壁13の上流側表面とその内部間隙中に付
着したすすを低温酸化して除去する。また排気ガス中
の、NOxをはじめとするガス状汚染物質を酸化・還元
して除去する。When a high frequency high voltage or a high voltage pulse voltage is continuously or intermittently applied from the AC power source 10 between the plasma processing electrodes 8 and 9, the upstream end 23 of the wire electrode element 22 and the wire mesh electrode. Silent discharge is generated between the element 22 through the upstream ceramic closing part 15 which is a dielectric and the upstream opening 19 of the ceramic partition wall 13, and the radicals generated thereby generate the radicals in the upstream opening. The soot advancing into each upstream gas passage group 17 from 19 and adhering to the upstream surface of the ceramic partition wall 13 and its internal gap is oxidized at low temperature and removed. Also, it removes gaseous pollutants such as NOx in the exhaust gas by oxidizing and reducing them.
【0029】図4は本発明の図3と異なる実施例24の
主要部の縦断面図で、上流側プラズマ処理電極8は本実
施例では針金電極要素25よりなり、その下流側先端部
26が上記上流側開口部19の開口中心付近に位置す
る。それ以外の12から23までの要素の名称および機
能は図3の実施例12における同一番号の要素と同様で
ある。FIG. 4 is a longitudinal sectional view of the main part of a twenty-fourth embodiment of the present invention, which is different from FIG. 3, in which the upstream plasma processing electrode 8 is composed of a wire electrode element 25 in this embodiment, and the downstream tip 26 thereof. It is located near the center of the opening of the upstream opening 19. The names and functions of the other elements 12 to 23 are the same as those of the elements with the same numbers in the twelfth embodiment of FIG.
【0030】両電極8、9の間に交流電源10より上記
交流電圧を印加すると、該上流側先端部26と下流側先
端部23の間に無声放電が発生してラジカルが生成、上
流側開口部19付近で先ずすすの酸化がスタートし、逐
次上流側ガス通路17の内部に及ぶ。その作用を助ける
ため、図には示されていないプラズマ処理電極8の該針
金電極要素を上記上流側ガス通路17の内部に挿入し、
また抽出する挿入・抽出手段があり、すすの酸化除去の
進行と共に逐次該上流側先端部26を進行させ、またす
すの除去がおわればこれをもとの位置に抽出する。When the AC voltage is applied between the electrodes 8 and 9 from the AC power source 10, silent discharge is generated between the upstream side tip portion 26 and the downstream side tip portion 23 to generate radicals and the upstream side opening. The soot oxidation first starts in the vicinity of the portion 19 and successively reaches the inside of the upstream gas passage 17. In order to assist its action, the wire electrode element of the plasma processing electrode 8 not shown in the figure is inserted into the inside of the upstream gas passage 17,
Further, there is an inserting / extracting means for extracting, and the upstream end portion 26 is successively advanced as the soot is oxidized and removed, and when the soot is removed, the soot is extracted to the original position.
【0031】なおこの場合ラジカルの作用でNOxを始
めとするガス状汚染物質も除去されることは既に記した
通りである。As described above, in this case, NOx and other gaseous pollutants are also removed by the action of radicals.
【0032】図5は本発明の図3および図4と異なる実
施例27の主要部の縦断面図で、上流側プラズマ処理電
極8は図4と同様に針金電極要素25よりなる。しかし
本実施例ではこの針金電極要素25は該上流側ガス通路
群17内に奥まで上流側から挿入されており、該下流側
ガス通路群18内に下流側から奥まで挿入された下流側
プラズマ処理電極9の針金電極要素22と該多孔質隔壁
13を介して対向している。それ以外の8から25まで
の要素の名称および機能は図3および図4の実施例1
2、24における同一番号の要素と同様である。FIG. 5 is a longitudinal sectional view of the main part of a twenty-seventh embodiment of the present invention, which is different from FIGS. 3 and 4, and the upstream plasma processing electrode 8 is composed of a wire electrode element 25 as in FIG. However, in the present embodiment, the wire electrode element 25 is inserted into the upstream side gas passage group 17 from the upstream side to the back side, and the downstream side plasma inserted into the downstream side gas passage group 18 from the downstream side to the back side. It faces the wire electrode element 22 of the processing electrode 9 via the porous partition wall 13. The names and functions of the other elements 8 to 25 are the same as those in the first embodiment shown in FIGS. 3 and 4.
This is the same as the elements with the same numbers in 2 and 24.
【0033】いま両電極8、9の間に交流電源10より
上記交流電圧を供給すると、上記の両針金電極要素2
2、25間に該多孔質隔壁13を介して放電が発生し、
該隔壁の上流側表面ならびに内部空隙内に付着したすす
が除去され、かつNOxを始めとするガス状汚染物質も
除去されることは既に記した通りである。When the AC voltage is applied between the electrodes 8 and 9 from the AC power supply 10, the wire electrode elements 2 are
A discharge is generated between the 2 and 25 through the porous partition wall 13,
As described above, the soot adhering to the upstream surface of the partition wall and the inside voids is removed, and the gaseous pollutants including NOx are also removed.
【0034】図6は本発明の図3、図4および図4と異
なる実施例28の主要部の縦断面図である。本実施例で
は2組のプラズマ処理電極9、29のいずれもが該下流
側ガス通路群18内に下流側から奥まで挿入された針金
電極要素22および30よりなり、且つ両針金電極要素
22、30はそれぞれ中間に1つの上流側ガス通路14
とその両側の該多孔質セラミック隔壁13を介して対向
している。それ以外の9から22までの要素の名称およ
び機能は図3、図4およびの実施例12、24、28に
おける同一番号の要素と同様である。FIG. 6 is a vertical cross-sectional view of the main part of an embodiment 28 of the present invention, which is different from FIGS. 3, 4 and 4. In this embodiment, each of the two sets of plasma treatment electrodes 9 and 29 is composed of wire electrode elements 22 and 30 inserted from the downstream side to the inside in the downstream gas passage group 18, and both wire electrode elements 22 and 30 is one upstream gas passage 14 in the middle
And the porous ceramic partition walls 13 on both sides thereof are opposed to each other. The names and functions of the other elements 9 to 22 are the same as those of the elements with the same numbers in FIGS. 3 and 4 and the embodiments 12, 24, and 28.
【0035】いま両プラズマ処理電極9、29の間に交
流電源10より上記交流電圧を印加すると、上記両針金
電極要素22、30の間に、これらに挟まれた該上流側
ガス通路14とその両側の該多孔質セラミック隔壁13
を介して無声放電が発生し、すすとガス状汚染物質が除
去されることは上記の通りである。When the AC voltage is applied from the AC power supply 10 between the plasma processing electrodes 9 and 29, the upstream gas passage 14 sandwiched between the wire electrode elements 22 and 30 and the upstream gas passage 14 therebetween. The porous ceramic partition walls 13 on both sides
As described above, the silent discharge is generated through the soot and the gaseous pollutants are removed by the soot.
【0036】[0036]
【効果】本発明は上述の通りであるので、セラミックフ
ィルターのフィルター要素の上流側表面および内部空隙
に付着したすすを放電によるプラズマ処理によって常時
酸化分解し、その圧力損失のすす付着による上昇を防止
してデイーゼルエンジンの効率低下を防ぎ、かつセラミ
ックフィルターの寿命を長く維持する事ができる。[Advantages] Since the present invention is as described above, the soot adhering to the upstream surface and internal voids of the filter element of the ceramic filter is constantly oxidatively decomposed by the plasma treatment by electric discharge, and the increase of the pressure loss due to the soot adhesion is prevented. As a result, the efficiency of the diesel engine can be prevented from decreasing and the life of the ceramic filter can be maintained for a long time.
【0037】また同時にデイーゼルエンジン排気ガス中
に含まれるNOxをはじめとするガス状汚染物質をプラ
ズマ処理によって酸化・還元し、これを除去できて極め
て経済的なデイーゼルエンジン排気ガスの浄化が達成で
きる。At the same time, gaseous pollutants such as NOx contained in the exhaust gas of the diesel engine can be oxidized and reduced by the plasma treatment, and can be removed to achieve extremely economical purification of the exhaust gas of the diesel engine.
【0038】[0038]
【図面の簡単な説明】[Brief description of drawings]
【図1】この発明の基本概念を示す実施例の縦断面図で
ある。FIG. 1 is a vertical sectional view of an embodiment showing the basic concept of the present invention.
【図2】この発明に用いられるハニカム型セラミックフ
ィルターの斜視図である。FIG. 2 is a perspective view of a honeycomb type ceramic filter used in the present invention.
【図3】この発明の別の実施例の縦断面図である。FIG. 3 is a vertical sectional view of another embodiment of the present invention.
【図4】この発明の更に別の実施例の縦断面図である。FIG. 4 is a vertical sectional view of still another embodiment of the present invention.
【図5】この発明の更に別の実施例の縦断面図である。FIG. 5 is a vertical sectional view of still another embodiment of the present invention.
【図6】この発明の更に別の実施例の縦断面図である。FIG. 6 is a vertical sectional view of still another embodiment of the present invention.
2 排気ダクト 3 ガス入口 4 ガス出口 5 ケーシング 6 セラミックフィルター 7 フィルター要素 8 上流側プラズマ処理電極 9 下流側プラズマ処理電極 10 交流電源 11 ハニカム型セラミックフィルター 13 多孔質セラミック隔壁 17 上流側ガス通路群 18 下流側ガス通路群 21 金網電極要素 22 針金電極要素 25 針金電極要素 29 下流側プラズマ処理電極 2 Exhaust Duct 3 Gas Inlet 4 Gas Outlet 5 Casing 6 Ceramic Filter 7 Filter Element 8 Upstream Plasma Treatment Electrode 9 Downstream Plasma Treatment Electrode 10 AC Power Supply 11 Honeycomb Ceramic Filter 13 Porous Ceramic Partition 17 Upstream Gas Passage Group 18 Downstream Side gas passage group 21 Wire mesh electrode element 22 Wire electrode element 25 Wire electrode element 29 Downstream plasma treatment electrode
Claims (10)
スの出口を有するケーシングの内部に、ガス流を遮る如
くに多孔質セラミックのフィルター要素よりなるセラミ
ックフィルターを設け、該フィルター要素を挟んで、ガ
スの流れを妨げない構造の少なくとも1つの電極要素か
らなるプラズマ処理電極の2組を相互に絶縁のうえ配設
し、この両プラズマ処理電極に接続してその間に交流電
圧を印加するための交流電源を設け、該フィルター要素
の少なくとも1部を介して両プラズマ処理電極間に放電
を発生させる事を特徴とするデイーゼルエンジン排気ガ
ス浄化装置。1. A ceramic filter made of a porous ceramic filter element is provided inside a casing having an inlet for exhaust gas containing soot and an outlet for clean gas, and the filter element is sandwiched between the ceramic filters. , For arranging two sets of plasma processing electrodes consisting of at least one electrode element having a structure that does not impede the flow of gas so as to be insulated from each other, and connecting the two plasma processing electrodes to apply an AC voltage therebetween. An exhaust gas purifying apparatus for a diesel engine, characterized in that an AC power source is provided, and an electric discharge is generated between both plasma processing electrodes through at least a part of the filter element.
ミックフィルターに近接して、その上流側と下流側に設
けられた金網ないし多孔板のいずれかの電極要素から成
る事を特徴とする請求項1に記載のデイーゼルエンジン
排気ガス浄化装置。2. The plasma processing electrodes are composed of an electrode element, which is either a wire mesh or a perforated plate, which is provided in the upstream side and the downstream side of the ceramic filter in the vicinity of the ceramic filter. Exhaust gas purification device for diesel engine described in.
造で多数の細長いガス通路群より成ると共に、そのガス
通路の上流端と下流端が交互にセラミックよりなる閉塞
部で閉塞されて、上流側に連通した上流側ガス通路群と
下流側に連通した下流側ガス通路群に分かれ、その隣合
う両ガス通路の間の隔壁が上記フィルター要素を構成し
た、ハニカム型セラミックフィルターである事を特徴と
する請求項1または2のいずれか1項に記載のデイーゼ
ルエンジン排気ガス浄化装置。3. The ceramic filter has a honeycomb structure and is composed of a large number of elongated gas passage groups, and the upstream and downstream ends of the gas passages are alternately closed by a closed portion made of ceramic to communicate upstream. 2. A honeycomb type ceramic filter, which is divided into a side gas passage group and a downstream side gas passage group communicating with the downstream side, and a partition wall between adjacent gas passages constitutes the filter element. Alternatively, the diesel engine exhaust gas purifying device according to any one of 2 or 3.
一方のが上記ハニカム型セラミックフィルターの閉塞端
の上流側に、これに近接して設けられた金網ないし多孔
板のいずれかの電極要素から成り、他方が上記ハニカム
型セラミックフィルターの該下流側ガス通路群に下流側
から奥まで挿入された針金状の電極要素から成る事を特
徴とする請求項3に記載のデイーゼルエンジンの排気ガ
ス浄化装直。4. Of the two sets of plasma treatment electrodes,
One is composed of an electrode element of either a wire mesh or a perforated plate provided on the upstream side of the closed end of the honeycomb type ceramic filter and adjacent thereto, and the other is the gas passage on the downstream side of the honeycomb type ceramic filter. The exhaust gas purification refurbishment of a diesel engine according to claim 3, characterized by comprising wire-shaped electrode elements inserted into the group from the downstream side to the inner side.
一方が上記ハニカム型セラミックフィルターの上流側ガ
ス通路群の入口付近に下流側先端部を位置する如くに配
設された針金状の電極要素から成り、他方が該下流側ガ
ス通路群内に下流側から挿入された針金状の電極要素か
ら成る事を特徴とする請求項3に記載のデイーゼルエン
ジンの排気ガス浄化装置。5. Of the two sets of plasma treatment electrodes,
One consists of wire-shaped electrode elements arranged so that the downstream tip is located near the inlet of the upstream gas passage group of the honeycomb ceramic filter, and the other consists of the downstream side in the downstream gas passage group. The exhaust gas purifying device for a diesel engine according to claim 3, wherein the exhaust gas purifying device comprises a wire-shaped electrode element inserted from the inside.
一方が上記ハニカム型セラミックフィルターの該上流側
ガス通路群のそれぞれの入口付近に下流側先端部を位置
する如くに配設された針金状の電極要素からなり、他方
が該下流側ガス通路群に下流側から挿入された針金状の
電極要素から成り、かつ該上流側処理電極の針金状電極
要素をそれぞれその先端が対向する該上流側ガス通路の
入口から該ガス通路内に挿入・抽出する挿入・抽出手段
を設けた事を特徴とする請求項5に記載のデイーゼルエ
ンジンの排気ガス浄化装置。6. Of the two sets of plasma treatment electrodes,
One consists of wire-shaped electrode elements arranged so that the downstream tip is located near the respective inlets of the upstream gas passage group of the above-mentioned honeycomb type ceramic filter, and the other consists of the downstream gas passage group. Insertion consisting of wire-like electrode elements inserted from the downstream side, and inserting / extracting the wire-like electrode elements of the upstream processing electrode into the gas passages from the inlets of the upstream gas passages whose tips respectively face each other. An exhaust gas purifying device for a diesel engine according to claim 5, characterized in that extraction means is provided.
一方が上記ハニカム型セラミックフィルターの該上流側
ガス通路群内に上流側から奥まで挿入された針金状の電
極要素から成り、他方が該下流側ガス通路群内に下流側
から奥まで挿入された針金状の電極要素から成る事を特
徴とする請求項3に記載のデイーゼルエンジンの排気ガ
ス浄化装置。7. Of the two sets of plasma treatment electrodes,
One consists of wire-shaped electrode elements inserted from the upstream side to the inside of the upstream side gas passage group of the honeycomb ceramic filter, and the other is inserted from the downstream side to the inside of the downstream side gas passage group. The exhaust gas purifying apparatus for a diesel engine according to claim 3, wherein the exhaust gas purifying apparatus comprises a wire-shaped electrode element.
該下流側ガス通路群内に下流側から挿入された針金状の
電極要素から成り、かつ両組のプラズマ処理電極に属す
る電極要素が互いに1つの上記上流側ガス通路を介して
対向配設された事を特徴とする請求項3に記載のデイー
ゼルエンジンの排気ガス浄化装置。8. Both of the two sets of plasma processing electrodes are wire-like electrode elements inserted from the downstream side into the downstream gas passage group, and the electrode elements belonging to both sets of plasma processing electrodes are mutually The exhaust gas purifying apparatus for a diesel engine according to claim 3, wherein the exhaust gas purifying apparatus is opposed to each other via one of the upstream gas passages.
V以上、出力周波数5kHz以上の高周波高電圧を発生
する高周波高圧電源であるた事を特徴とする請求項1〜
8のいずれか1項に記載のデイーゼルエンジンの排気ガ
ス浄化装置。9. The above AC power supply has an output voltage peak value of 3 k.
A high-frequency high-voltage power supply that generates a high-frequency high voltage of V or more and an output frequency of 5 kHz or more.
8. An exhaust gas purifying device for a diesel engine according to any one of 8 above.
V以上、出力周波数50Hz以上のパルス状高電圧を発
生する高圧パルス電源であるた事を特徴とする請求項1
〜8のいずれか1項に記載のデイーゼルエンジンの排気
ガス浄化装置。10. The above AC power supply has an output voltage peak value of 5 k.
2. A high-voltage pulse power supply that generates a pulsed high voltage of V or higher and an output frequency of 50 Hz or higher.
9. An exhaust gas purifying device for a diesel engine according to any one of items 1 to 8.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4350104A JPH06146852A (en) | 1992-11-13 | 1992-11-13 | Diesel engine exhaust gas purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4350104A JPH06146852A (en) | 1992-11-13 | 1992-11-13 | Diesel engine exhaust gas purifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH06146852A true JPH06146852A (en) | 1994-05-27 |
Family
ID=18408264
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4350104A Pending JPH06146852A (en) | 1992-11-13 | 1992-11-13 | Diesel engine exhaust gas purifying device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06146852A (en) |
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| JP2002339731A (en) * | 2001-05-18 | 2002-11-27 | Mitsubishi Heavy Ind Ltd | Method and device for treatment of engine exhaust emission |
| JP2003035128A (en) * | 2001-07-19 | 2003-02-07 | Toyota Central Res & Dev Lab Inc | Exhaust gas purification device for internal combustion engine |
| EP1277928A1 (en) * | 2001-07-19 | 2003-01-22 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Exhaust gas purifying apparatus for internal combustion engines |
| JP2003049632A (en) * | 2001-08-03 | 2003-02-21 | Nippon Kouatsu Electric Co | Particulate matter removing method and its device |
| JP2003103130A (en) * | 2001-09-28 | 2003-04-08 | Nippon Kouatsu Electric Co | Method and apparatus for removing particulate matter |
| KR20030027407A (en) * | 2001-09-28 | 2003-04-07 | 현대자동차주식회사 | Post treatment exhaust contamination gas decreasing system in diesel engine |
| JP2005531401A (en) * | 2002-07-03 | 2005-10-20 | シーメンス アクチエンゲゼルシヤフト | Plasma soot filter |
| KR100482701B1 (en) * | 2002-07-12 | 2005-04-13 | 주식회사 세실플라즈마 | Apparatus and method for cleaning of exahust gas with low temperature plasma |
| WO2004013469A1 (en) * | 2002-08-05 | 2004-02-12 | Ngk Insulators, Ltd. | Exhaust gas treating apparatus |
| US7442218B2 (en) | 2002-08-05 | 2008-10-28 | Ngk Insulators, Ltd. | Exhaust gas treatment apparatus |
| EP1441112A1 (en) * | 2003-01-15 | 2004-07-28 | Toyota Jidosha Kabushiki Kaisha | An exhaust gas purifying apparatus |
| US7514047B2 (en) | 2003-01-15 | 2009-04-07 | Toyota Jidosha Kabushiki Kaisha | Exhaust gas purifying apparatus |
| WO2006028322A1 (en) * | 2004-09-07 | 2006-03-16 | Neophotech, Inc. | Apparatus for purifying diesel exhaust gas with coated photocatalyst layer and electrode, and manufacturing method thereof |
| CN100356041C (en) * | 2005-05-20 | 2007-12-19 | 中国科学院金属研究所 | Carbon black filtering and electric direct-heating type regeneration device for diesel truck |
| WO2007023267A1 (en) * | 2005-08-25 | 2007-03-01 | Perkins Engines Company Limited | Autoselective regenerating particulate filter |
| GB2429417A (en) * | 2005-08-25 | 2007-02-28 | Perkins Engines Co Ltd | Autoselective regenerating particulate filter |
| GB2429417B (en) * | 2005-08-25 | 2010-08-11 | Perkins Engines Co Ltd | Autoselective regenerating particulate filter |
| US8388711B2 (en) | 2005-08-25 | 2013-03-05 | Perkins Engine Company Ltd. | Autoselective regenerating particulate filter |
| JP2007098311A (en) * | 2005-10-05 | 2007-04-19 | Daihatsu Motor Co Ltd | Electrode for plasma reactor |
| JP2012504039A (en) * | 2008-09-30 | 2012-02-16 | パーキンズ エンジンズ カンパニー リミテッド | Method and apparatus for regenerating a filter |
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