JPH0249914A - Exhaust gas purifying method for diesel engine - Google Patents
Exhaust gas purifying method for diesel engineInfo
- Publication number
- JPH0249914A JPH0249914A JP63198657A JP19865788A JPH0249914A JP H0249914 A JPH0249914 A JP H0249914A JP 63198657 A JP63198657 A JP 63198657A JP 19865788 A JP19865788 A JP 19865788A JP H0249914 A JPH0249914 A JP H0249914A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- exhaust gas
- gas
- diesel engine
- soot
- 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
- 238000000034 method Methods 0.000 title claims description 24
- 239000007789 gas Substances 0.000 claims abstract description 67
- 239000000567 combustion gas Substances 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 238000002485 combustion reaction Methods 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 10
- 238000000746 purification Methods 0.000 claims description 3
- 239000004071 soot Substances 0.000 abstract description 22
- 239000000428 dust Substances 0.000 abstract description 21
- 238000011069 regeneration method Methods 0.000 abstract description 15
- 230000008929 regeneration Effects 0.000 abstract description 14
- 230000003647 oxidation Effects 0.000 abstract description 5
- 238000007254 oxidation reaction Methods 0.000 abstract description 5
- 230000003584 silencer Effects 0.000 abstract description 4
- 230000001172 regenerating effect Effects 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 238000011144 upstream manufacturing Methods 0.000 abstract description 2
- 239000000779 smoke Substances 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Processes For Solid Components From Exhaust (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ディーゼル機関の排ガス浄化方法に係り、特
に排ガス中の煤塵を除去するフィルタを再生するのに好
適なディーゼル機関の排ガス浄化方法に関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method for purifying exhaust gas from a diesel engine, and more particularly to a method for purifying exhaust gas from a diesel engine suitable for regenerating a filter for removing soot and dust from exhaust gas. .
ディーゼル機関開発の歴史は古く、現在までの改良によ
って重質油を燃料として使用でき、動力転換率の高い内
燃機関としてほぼ技術が完熟している。ところがディー
ゼル機関の欠点は、排ガス中に窒素酸化物と煤塵が含ま
れている点にある。The development of diesel engines has a long history, and improvements made to date have made it possible to use heavy oil as fuel, and the technology has almost reached maturity as an internal combustion engine with a high power conversion ratio. However, the disadvantage of diesel engines is that the exhaust gas contains nitrogen oxides and soot.
これは燃焼時の高熱で発生するものであり、機関効率を
よくするほど多く発生する傾向にあって発生の抑制は困
難である。This occurs due to the high heat during combustion, and as the efficiency of the engine increases, it tends to occur more frequently, making it difficult to suppress its occurrence.
最近、都市部における大気汚染の問題から自動車用、自
家発電用などの内燃機関から発生する排ガスが規制され
る傾向にあり、ディーゼル機関の排ガスにおいても煤塵
を低減する必要がある。煤塵を除去する技術として電気
集塵器を用いる方法、サイクロンを用いる方法、フィル
タを用いる方法が提案されているか、性能と装置の大き
さからフィルタを用いる方法が実用化されている。Recently, due to the problem of air pollution in urban areas, there is a tendency to regulate the exhaust gas generated from internal combustion engines for automobiles, private power generation, etc., and it is necessary to reduce soot and dust in the exhaust gas from diesel engines as well. As techniques for removing soot and dust, methods using an electric precipitator, a method using a cyclone, and a method using a filter have been proposed, and a method using a filter has been put into practical use due to the performance and size of the device.
排ガス中の煤塵をフィルタで捕捉して除去する場合、フ
ィルタが徐々に閉塞するので詰まった煤塵を除去する再
生処理が必要である。ディーゼル排ガス処理に特有な再
生方法として、詰まった煤塵を燃焼させて消去する方法
がある。フィルタ上の煤塵は、通常500℃以上の温度
で酸化され消去する。触媒が存在すれば酸化温度を低下
させることも可能である。したがって、一定以上の温度
にフィルタを保持できれば、煤塵の捕集と消去を同時に
行なうことが可能である。しかし、実際には−・定以上
の温度を常時保持するのは困難であり、触媒の劣化の問
題もあり、煤塵を捕集して閉塞したフィルタを人為的に
加熱して燃焼させ、再生することが多い。When soot and dust in exhaust gas is captured and removed by a filter, the filter gradually becomes clogged, so a regeneration process is required to remove the clogged soot and dust. A regeneration method unique to diesel exhaust gas treatment involves burning and eliminating clogged soot and dust. The soot and dust on the filter is usually oxidized and erased at a temperature of 500° C. or higher. It is also possible to lower the oxidation temperature if a catalyst is present. Therefore, if the filter can be maintained at a temperature above a certain level, it is possible to simultaneously collect and eliminate soot and dust. However, in reality, it is difficult to maintain a constant temperature above a certain level, and there is also the problem of deterioration of the catalyst.Soot and dust are collected and the clogged filter is artificially heated and burned to regenerate it. There are many things.
煤塵で閉塞したフィルタを加熱して再生する際、まず炭
素粒子に吸着されたタール等の揮発物質が蒸発して温度
が上昇した後に着火し、次いで不完全燃焼により一酸化
炭素等を発生し、さらに昇温した後に完全燃焼する。こ
の過程で発生する多核芳香族化合物等は有害で発癌性も
あり、大気に放出すると2次公害を引き起こす。When a filter clogged with soot and dust is heated and regenerated, volatile substances such as tar adsorbed on carbon particles evaporate and the temperature rises, which then ignites, and then incomplete combustion generates carbon monoxide, etc. Complete combustion occurs after the temperature rises further. Polynuclear aromatic compounds generated in this process are harmful and even carcinogenic, and when released into the atmosphere, they cause secondary pollution.
〔発明が解決しようとする課題〕
フィルタ再生時に発生する有害な揮発成分を除去する方
法として提案された特開昭60−20491°3号公報
に示された方法では、フィルタ下流側の貴金属触媒で酸
化する方法を採用している。[Problem to be solved by the invention] In the method proposed in Japanese Patent Application Laid-open No. 60-20491°3, which was proposed as a method for removing harmful volatile components generated during filter regeneration, a noble metal catalyst downstream of the filter is used. An oxidation method is used.
しかし、触媒を用いる上記従来技術は、排ガス温度低下
時に一旦触媒表面がタールに覆われ、排ガス中の酸素か
ら遮断されてしまうと、酸化可能温度まで昇温しても排
ガス中の揮発分だけでなく、触媒表面のタールも酸化し
難くなるという欠点があり、また長期の使用により性能
が劣化するという問題があった。However, with the above conventional technology that uses a catalyst, once the catalyst surface is covered with tar when the exhaust gas temperature drops and is cut off from oxygen in the exhaust gas, even if the temperature rises to the temperature where it can be oxidized, only volatile matter in the exhaust gas remains. However, there was a problem that the tar on the surface of the catalyst was difficult to oxidize, and the performance deteriorated with long-term use.
特開昭59−77021号公報では、エンジン排ガス中
の煤塵で閉塞したフィルタを、別個に設置したバーナか
らの燃焼ガスで焼却し、焼却ガスはディーゼル機関人口
に供給するという方法を採用し、煤塵燃焼ガスによる公
害や上記課題を解決している。しかし、この方法では煤
塵の焼却はフィルタ全体にわたり一度に行なわれるので
、焼却時のエンジン入口ガス組成は煤塵焼却をしないと
きに比し大幅に変動し、ディーゼル機関の運転状態を均
一に保持することが困難であった。Japanese Patent Application Laid-Open No. 59-77021 adopts a method in which a filter clogged with soot in engine exhaust gas is incinerated with combustion gas from a separately installed burner, and the incinerated gas is supplied to the diesel engine population. This solves the problem of pollution caused by combustion gas and the above issues. However, in this method, the soot and dust are incinerated over the entire filter at once, so the engine inlet gas composition during incineration varies significantly compared to when no soot and dust is incinerated, making it difficult to maintain a uniform operating condition of the diesel engine. was difficult.
上記した従来技術の課題は、ディーゼル機関の排ガス中
の炭素質微粒子をフィルタにより捕集する工程と、炭素
質微粒子を捕集したフィルタを加熱して炭素質微粒子を
焼却する工程と、焼却された炭素′1.重粒子の燃焼ガ
スを吸引する工程と、吸引された燃焼ガスをディーゼル
機関の入口吸気管に戻す工程とからなるディーゼル機関
の排ガス浄化方法において、上記焼却工程と吸引工程を
フィルタの一部の同一部分について実施しつつフィルタ
上を順次移動させることを特徴とするディーゼル機関の
排ガス浄化方法により解決される。The problems with the conventional technology described above are the process of collecting carbonaceous particles in the exhaust gas of a diesel engine with a filter, the process of heating the filter that has collected the carbonaceous particles to incinerate the carbonaceous particles, and the process of incinerating the carbonaceous particles. Carbon'1. In a diesel engine exhaust gas purification method that includes a step of sucking combustion gas containing heavy particles and a step of returning the sucked combustion gas to the inlet intake pipe of the diesel engine, the incineration step and the suction step are performed in the same part of the filter. This problem is solved by a method for purifying exhaust gas of a diesel engine, which is characterized by sequentially moving the exhaust gas on the filter while performing the cleaning on each section.
本発明では、フィルタの面上で加熱手段と加熱によって
発生するガスを吸引する手段の位置が少しずつ移動する
ので、フィルタによる煤塵除去と、フィルタに詰まった
煤塵の酸化除去が定常状態で行なわれる。したがって、
再生に使用した後のディーゼル機関に戻すガス組成と流
量も一定であり、ディーゼル機関の運転も一定に維持さ
れる。再生に使用した後のガス中の有害成分は、ディー
ゼル機関゛で他の燃料とともに燃焼し無害化する。In the present invention, the positions of the heating means and the means for suctioning the gas generated by heating are moved little by little on the surface of the filter, so that the filter removes soot and dust and oxidizes and removes the soot and dust clogging the filter in a steady state. . therefore,
The gas composition and flow rate returned to the diesel engine after being used for regeneration are also constant, and the operation of the diesel engine is also maintained constant. Harmful components in the gas after being used for regeneration are combusted with other fuels in a diesel engine and rendered harmless.
第1A図は、本発明の一実施例の全体系統図である。第
1A図において、1はエアクリーナ、2はディーゼル機
関、3は排ガス用浄化器、4は消音器、5は吸気管、6
はディーゼル出口煙道、7はフィルタ出口煙道、8は吸
引管、9は吸引ガス調整用バルブである。第1B図は、
第1A図の排ガス用浄化器の拡大説明図である。第1図
において、ディーゼル機関2で発生した排ガスは、フィ
ルタ13が設置された排ガス用浄化器3で煤塵が除去さ
れ、消音器4を通って大気中へ放出される。FIG. 1A is an overall system diagram of one embodiment of the present invention. In FIG. 1A, 1 is an air cleaner, 2 is a diesel engine, 3 is an exhaust gas purifier, 4 is a silencer, 5 is an intake pipe, 6
7 is a diesel outlet flue, 7 is a filter outlet flue, 8 is a suction pipe, and 9 is a suction gas adjustment valve. Figure 1B shows
FIG. 1A is an enlarged explanatory view of the exhaust gas purifier shown in FIG. 1A. In FIG. 1, exhaust gas generated by a diesel engine 2 has soot and dust removed by an exhaust gas purifier 3 equipped with a filter 13, and is discharged into the atmosphere through a muffler 4.
本発明の特徴として、排ガス用浄化器3の一部分の排ガ
スを吸引し、ディーゼル機関2の入口にリサイクルさせ
る吸引管8が設置されている。吸引管8では、ディーゼ
ル機関2の入口が負圧であり出口が正圧であるので、吸
引ガス調整用バルブってガス流量を調整すれば、常時排
ガスがリサイクルされる。As a feature of the present invention, a suction pipe 8 is installed to suck in a portion of the exhaust gas from the exhaust gas purifier 3 and recycle it to the inlet of the diesel engine 2. In the suction pipe 8, since the inlet of the diesel engine 2 has a negative pressure and the outlet has a positive pressure, the exhaust gas is constantly recycled by adjusting the gas flow rate using the suction gas adjustment valve.
第1B図において、ディーゼル出口煙道6より排ガス用
浄化器3に流入した排ガスは、フィルタ13を通過して
煤塵が捕集され浄化された(麦、フィルタ出口煙道7を
通って消音器に排出される。In Fig. 1B, the exhaust gas that has flowed into the exhaust gas purifier 3 from the diesel outlet flue 6 passes through the filter 13, where soot and dust is collected and purified. be discharged.
本実施例の特徴として、上下に移動する再生ガス吸引器
10があり、フィルタ13面上の再生ガス吸引器10の
位置に対応するフィルタ13上流の電熱ヒータ12が作
動し、電熱によってフィルタI3に流入するガスを、煤
塵の酸化に必要な温度まで加熱してフィルタ13を通し
、再生時に発生ずる2次公害物質を含むガスは再生ガス
吸引器10で吸引し、吸引管8によってディーゼル機関
2の入口(吸気管5)に戻している。再生ガス吸引器1
0の作用しない部分のフィルタI3は加熱もされず、排
ガス浄化に使用されており、再生ガス吸引器10がその
場所に移動するまで再生されない。A feature of this embodiment is that there is a regeneration gas suction device 10 that moves up and down, and the electric heater 12 upstream of the filter 13 corresponding to the position of the regeneration gas suction device 10 on the surface of the filter 13 is activated, and the electric heat is applied to the filter I3. The inflowing gas is heated to the temperature required for oxidizing the soot and dust and passed through the filter 13. The gas containing secondary pollutants generated during regeneration is sucked in by the regeneration gas suction device 10, and is then sent to the diesel engine 2 through the suction pipe 8. It is returned to the inlet (intake pipe 5). Regeneration gas suction device 1
The filter I3 in the non-active portion of 0 is not heated and is used for exhaust gas purification, and is not regenerated until the regeneration gas suction device 10 is moved to that location.
本発明になる排ガス用浄化器の他の実施例を第2図に示
す。本実施例では、再生ガス吸引器10は一定位置に固
定されており、フィルタ13がフィルタ回転軸15の周
りを回転して移動する。加熱源としてはLPGガス管1
管炉8のLPGガスと、燃焼用空気管19からの燃焼用
空気により高温ガス発生器17によって生じる高温ガス
を用いており、高温ガス発生器17としては通常のバー
ナの他、触媒バーナも好都合である。Another embodiment of the exhaust gas purifier according to the present invention is shown in FIG. In this embodiment, the regeneration gas suction device 10 is fixed at a fixed position, and the filter 13 rotates and moves around the filter rotation axis 15. LPG gas pipe 1 as a heating source
The high-temperature gas generated by the high-temperature gas generator 17 using the LPG gas from the tube furnace 8 and the combustion air from the combustion air pipe 19 is used, and as the high-temperature gas generator 17, in addition to a normal burner, a catalytic burner is also convenient. It is.
なお、本発明実施の注意事項として、フィルタ13上で
の酸化を局在下させるため、フィルタ13への煤塵の笛
積が少ないうちに再生することが必要である。多量の煤
塵がフィルタ13に蓄積され、厚い層を形成した後に酸
化させれば、発熱によって燃焼が拡大することがある。Note that when implementing the present invention, in order to localize the oxidation on the filter 13, it is necessary to regenerate the filter 13 while the accumulation of soot and dust is small. If a large amount of dust accumulates in the filter 13 and oxidizes after forming a thick layer, combustion may expand due to heat generation.
本発明によれば、フィルタの再生時に発生する2次公害
物質を、酸化触媒とかインラインバーナを用いず、かつ
ディーゼル機関の運転変動なしに焼却処分することがで
きる。さらに、派生的な効果としてフィルタの通風圧力
損失が変動しない。According to the present invention, secondary pollutants generated during filter regeneration can be incinerated without using an oxidation catalyst or an in-line burner and without changing the operation of the diesel engine. Furthermore, as a side effect, the filter ventilation pressure loss does not fluctuate.
第1A図は、本発明の一実施例の全体系統図、第1B図
は、第1A図の排ガス用浄化器の拡大図、第2図は、本
発明の他の実施例の排ガス用浄化器の拡大図である。
1・・・エアクリーナ、2・・・ディーゼル機関、3・
・・排ガス用浄化器、4・・・消音器、5・・・吸気管
、6・・・ディーゼル出口煙道、7・・・フィルタ出口
煙道、8・・・吸引管、9・・・吸引ガス調整用バルブ
、10・・・燃焼ガス吸引器、11・・・吸引器移動機
、12・・・電熱ヒータ、13・・・フィルタ。
代理人 弁理士 川 北 武 長
フィルタ回転軸
回転駆動機
高温ガス発生器
LPGガス管
燃焼用空気管
エアクリーナ
ディーゼル機関
排ガス用浄化器
消音器
吸気管
ディーゼル出口煙道
フィルり出口煙道
吸引管
吸引ガス調整用バルブ
燃焼ガス吸引器
】3:フィルタ
第
1A図
1B図FIG. 1A is an overall system diagram of an embodiment of the present invention, FIG. 1B is an enlarged view of the exhaust gas purifier of FIG. 1A, and FIG. 2 is an exhaust gas purifier of another embodiment of the present invention. It is an enlarged view of. 1...Air cleaner, 2...Diesel engine, 3.
... Exhaust gas purifier, 4... Silencer, 5... Intake pipe, 6... Diesel outlet flue, 7... Filter outlet flue, 8... Suction pipe, 9... Suction gas adjustment valve, 10... Combustion gas suction device, 11... Suction device moving device, 12... Electric heater, 13... Filter. Agent Patent Attorney Takeshi Kawakita Filter rotary shaft rotary drive machine High temperature gas generator LPG gas pipe Combustion air pipe Air cleaner Diesel engine exhaust gas purifier Silencer Suction pipe Diesel outlet Flue Filling outlet Flue Suction pipe Suction gas adjustment Valve combustion gas suction device] 3: Filter Fig. 1A Fig. 1B
Claims (1)
ルタにより捕集する工程と、炭素質微粒子を捕集したフ
ィルタを加熱して炭素質微粒子を焼却する工程と、焼却
された炭素質微粒子の燃焼ガスを吸引する工程と、吸引
された燃焼ガスをディーゼル機関の入口吸気管に戻す工
程とからなるディーゼル機関の排ガス浄化方法において
、上記焼却工程と吸引工程をフィルタの一部の同一部分
について実施しつつフィルタ上を順次移動させることを
特徴とするディーゼル機関の排ガス浄化方法。(1) The process of collecting carbonaceous particles in the exhaust gas of a diesel engine with a filter, the process of heating the filter that has collected the carbonaceous particles to incinerate the carbonaceous particles, and the combustion of the incinerated carbonaceous particles. In a diesel engine exhaust gas purification method comprising a step of sucking gas and a step of returning the sucked combustion gas to the inlet intake pipe of the diesel engine, the above-mentioned incineration step and suction step are performed on the same part of the filter. A method for purifying exhaust gas from a diesel engine, characterized by moving the exhaust gas sequentially over a filter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63198657A JPH0249914A (en) | 1988-08-09 | 1988-08-09 | Exhaust gas purifying method for diesel engine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63198657A JPH0249914A (en) | 1988-08-09 | 1988-08-09 | Exhaust gas purifying method for diesel engine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0249914A true JPH0249914A (en) | 1990-02-20 |
Family
ID=16394872
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63198657A Pending JPH0249914A (en) | 1988-08-09 | 1988-08-09 | Exhaust gas purifying method for diesel engine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0249914A (en) |
-
1988
- 1988-08-09 JP JP63198657A patent/JPH0249914A/en active Pending
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