JPS6361489B2 - - Google Patents
Info
- Publication number
- JPS6361489B2 JPS6361489B2 JP21057582A JP21057582A JPS6361489B2 JP S6361489 B2 JPS6361489 B2 JP S6361489B2 JP 21057582 A JP21057582 A JP 21057582A JP 21057582 A JP21057582 A JP 21057582A JP S6361489 B2 JPS6361489 B2 JP S6361489B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- filter
- combustion
- air
- particulates
- 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
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
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/24—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
- F01N3/30—Arrangements for supply of additional air
- F01N3/306—Preheating additional air
-
- 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
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features
- F01N13/011—Exhaust or silencing apparatus characterised by constructional features having two or more purifying devices arranged in parallel
- F01N13/017—Exhaust or silencing apparatus characterised by constructional features having two or more purifying devices arranged in parallel the purifying devices are arranged in a single housing
-
- 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
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/023—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
- F01N3/025—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using fuel burner or by adding fuel to exhaust
-
- 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
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/031—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters having means for by-passing filters, e.g. when clogged or during cold engine start
- F01N3/032—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters having means for by-passing filters, e.g. when clogged or during cold engine start during filter regeneration only
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Processes For Solid Components From Exhaust (AREA)
Description
【発明の詳細な説明】
本発明は、デイーゼル機関の排気ガス中のカー
ボン等を主体とする微粒子をフイルタで捕集し、
そして燃焼処理することにより、排気ガスの浄化
をはかりうるデイーゼル機関の排気ガス処理装置
に関するものである。[Detailed Description of the Invention] The present invention uses a filter to collect fine particles mainly composed of carbon in the exhaust gas of a diesel engine.
The present invention also relates to an exhaust gas treatment device for a diesel engine that can purify exhaust gas through combustion treatment.
従来、微粒子捕集用のフイルタにより排気ガス
中の微粒子を捕集する排気ガス処理装置が使用さ
れているが、この場合、長期間の使用によつてフ
イルタに目詰りをきたすため、フイルタをひんぱ
んに交換する必要があり、不経済であつた。 Conventionally, exhaust gas treatment equipment has been used that uses particulate filters to collect particulates in the exhaust gas. It was uneconomical because it had to be replaced.
そこで、耐熱性材料のフイルタを2個備え、こ
れら2個のフイルタへの排気ガスの流れを切換え
うる弁を備え、一方のフイルタに排気ガスを通過
させながら、微粒子を捕集し、かつ他方のフイル
タで、その捕集した微粒子を燃焼させる操作を交
互に行なうようにした特開昭57−79209号の発明
がなされている。 Therefore, two filters made of heat-resistant material are equipped with a valve that can switch the flow of exhaust gas to these two filters. An invention disclosed in Japanese Patent Application Laid-open No. 79209/1983 has been made in which the filter is used to alternately burn the collected particles.
即ち、上記の発明を第1図の概略側断面図によ
り説明すると、図示されていないデイーゼル機関
の排気ガスEは上記図中の左側より矢印のごとく
流入し、切換弁1により片側のフイルタ2Aに流
入し、排気ガスE中のカーボン微粒子が捕集され
る。 That is, to explain the above invention with reference to the schematic side sectional view of FIG. The carbon particles in the exhaust gas E are collected.
また、切換弁1の軸後部の弁開閉により、他の
フイルタ2B側に火炎口3よりバーナ燃焼による
残留空気をもつた高温ガスBが流入し、フイルタ
2Bで前回捕集したカーボン等の微粒子を酸化燃
焼させ、フイルタ2B後部で、その微粒子燃焼ガ
スGをフイルタ2Aよりの排気ガスEと合流し、
排出させることにより、クリーンな排気ガスEcが
得られるようになつている。 In addition, by opening and closing the valve at the rear of the shaft of the switching valve 1, high-temperature gas B containing residual air from burner combustion flows into the other filter 2B side from the flame port 3, removing fine particles such as carbon that were previously collected by the filter 2B. Oxidized combustion is performed, and the particulate combustion gas G is combined with the exhaust gas E from the filter 2A at the rear of the filter 2B.
By discharging it, clean exhaust gas E c can be obtained.
以上のごとくその入り側を仕切壁6で仕切られ
た2個のフイルタ2A,2Bによる微粒子捕集
と、捕集微粒子の燃焼とを切換弁1の切換により
交互に行なわせ、フイルタ2A,2Bによる捕集
と燃焼とを交互に実施し、デイーゼル機関の排気
ガスEのカーボンの微粒子を除去したクリーンな
排気ガスEcとし、矢印のごとく排気出口部5より
外部に排出している。 As described above, the collection of particulates by the two filters 2A, 2B, whose inlet sides are partitioned by the partition wall 6, and the combustion of the collected particulates are performed alternately by switching the switching valve 1, and the filters 2A, 2B The collection and combustion are carried out alternately, and the carbon particulates of the exhaust gas E of the diesel engine are removed to form a clean exhaust gas Ec , which is discharged to the outside from the exhaust outlet portion 5 as shown by the arrow.
しかしながら、上記第1図の右側の各フイルタ
2A,2B出側の合流部4及び排気出口部5以後
に、図示されていない排気管及び消音器等を取り
付けると、排気抵抗が増大し、排圧が上昇する。 However, if an exhaust pipe, a muffler, etc. (not shown) are installed after the merging section 4 and exhaust outlet section 5 on the outlet side of each of the filters 2A and 2B on the right side of FIG. 1, the exhaust resistance increases and the exhaust pressure rises.
この排圧の上昇は、機関回転数及び負荷等に関
係して変化し、この排圧の変化によりバーナ燃焼
器の排圧が変化したこととなり、バート燃焼器の
ブロワーによる送風量が低下し、バーナ燃焼その
ものが悪化し、かつ残留空気量が低下し、場合に
よつてはバーナ火炎中にカーボンを発生し、フイ
ルタ2Bで焼却するはずがかえつてフイルタ2B
を目詰りさせることがあり、更にはフイルタ2B
の目詰り過大のため、デイーゼル機関に過大排圧
がかかり、出力低下を起し黒煙発生をうながし、
逆にカーボン発生を促進し、排気ガス処理装置自
身が異常発生源となる場合がある。 This increase in exhaust pressure changes in relation to the engine speed and load, and this change in exhaust pressure causes a change in the exhaust pressure of the burner combustor, which reduces the amount of air blown by the blower of the Bart combustor. Burner combustion itself deteriorates, and the amount of residual air decreases, and in some cases, carbon is generated in the burner flame, which should be incinerated by filter 2B, but instead burns by filter 2B.
This may cause the filter 2B to become clogged.
Due to excessive clogging, excessive exhaust pressure is applied to the diesel engine, causing a drop in output and promoting the generation of black smoke.
On the contrary, it may promote carbon generation, and the exhaust gas treatment device itself may become a source of abnormality.
一方、上記と同様に、デイーゼル機関の排気ガ
スE中のカーボン及び他の微粒子を集積し処理す
るデイーゼル機関排ガス清浄器に関する特開昭54
−111010号の発明においては、転換弁と2個のフ
イルタ部材との間に、空気―燃料噴霧化用ノズル
及び点火手段が2個必要であり、また燃却中のフ
イルタの燃焼生成物を排出するために大きなフア
ンを要し、それだけ抵抗が大きくなるという問題
がある。 On the other hand, similar to the above, Japanese Patent Application Laid-open No. 54 (1983) relates to a diesel engine exhaust gas purifier that collects and processes carbon and other particulates in diesel engine exhaust gas E.
- In the invention of No. 111010, two air-fuel atomizing nozzles and ignition means are required between the converter valve and the two filter members, and the combustion products of the filter during combustion are discharged. There is a problem in that a large fan is required to do this, and the resistance increases accordingly.
更に、内燃機関の排気系に設けられるトラツパ
容器の内部を左右2つに分けて、その各々にトラ
ツパを配置すると共に、それぞれのトラツパはヒ
ータ手段によつて加熱可能とし、これらのトラツ
パの前方に、どちらか一方のトラツパを開、他方
を閉とする板材切換弁を配置し、かつその板材切
替弁に制御された量の排気ガスの通過を可能とす
る孔を穿設した排気ガス微粒子捕集装置に関する
特開昭59−92318号の発明がなされている。 Furthermore, the inside of the trapper container provided in the exhaust system of the internal combustion engine is divided into two parts, left and right, and a trapper is placed in each of them, and each trapper can be heated by a heater means, and a trapper is placed in front of these trappers. , Exhaust gas particulate collection in which a plate switching valve is arranged to open one trapper and close the other, and the plate switching valve has a hole that allows a controlled amount of exhaust gas to pass through. An invention related to the device is disclosed in Japanese Patent Application Laid-Open No. 59-92318.
しかしながら、この発明は内燃機関が定格出力
以下等のシリンダ内の燃焼に必要とする空気量が
燃料量に対して過剰にある場合に対するものであ
る。 However, the present invention is directed to a case where the amount of air required for combustion in the cylinder is excessive with respect to the amount of fuel, such as when the internal combustion engine has a rated output or less.
即ち、内燃機関の排気ガス中に残留空気が充分
残つている場合のカーボン捕集及びその排気ガス
中の残留空気が板材切替弁を閉とし、板材切替弁
の孔よりカーボン燃焼用空気として排気ガスを少
量通過させ、燃焼促進のためヒータ加熱を行なわ
せるものである。 In other words, carbon is collected when there is sufficient residual air left in the exhaust gas of the internal combustion engine, and the residual air in the exhaust gas closes the plate material switching valve, and the exhaust gas is released from the hole in the plate material switching valve as carbon combustion air. A small amount of gas is passed through and heated by a heater to promote combustion.
一般に、デイーゼル機関の定格出力時には、燃
料の燃焼に必要な理論空気の1.5から1.6倍の空燃
比を有しているので、上記の方式が可能である。 Generally, at the rated output of a diesel engine, the air-fuel ratio is 1.5 to 1.6 times the theoretical air required for fuel combustion, so the above method is possible.
しかしながら、燃焼室内での空気利用効率を上
げる高出力デイーゼル機関では、理論空気の1.3
から1.4倍以下の空燃比になり、フイルタ内のカ
ーボンを再燃焼させる過剰空気をもつた排気ガス
の排出はなく、空燃比が少なくなる程多量のカー
ボンが発生し、そのカーボンがフイルタに捕集さ
れ、かつその焼却力が落ち、フイルタの抵抗が大
となり、そのデイーゼル機関は排気ブレーキ作用
を受け、増々カーボンが発生するという悪循環が
行なわれることになる。 However, in high-output diesel engines that increase air usage efficiency in the combustion chamber, the theoretical air
The air-fuel ratio becomes 1.4 times or less, and there is no exhaust gas with excess air that re-burns the carbon in the filter.The lower the air-fuel ratio, the more carbon is generated, and that carbon is collected in the filter. In addition, the incineration power decreases, the resistance of the filter increases, and the diesel engine is subjected to exhaust braking action, creating a vicious cycle in which more and more carbon is generated.
一方、前記第1図には図示されていないが、高
温ガスBを排気ガスE中のカーボンを捕集したフ
イルタ2A、または2Bにバーナ火炎口3より流
入させるための燃焼器としては、通常モータ駆動
による新規空気吸入用のフアン、燃料流入管及び
点火プラグを有するバーナが使用されるが、上記
の微粒子を焼却する際に、バーナ火炎、あるいは
電気ヒータで焼却用空気温度を500℃から800℃程
度に上昇させており、その新規空気は外気のた
め、その空気自身の温度上昇に必要とする燃料が
余分に消費され、それだけデイーゼル機関全体と
しての燃料消費量が増大するという問題がある。 On the other hand, although not shown in FIG. 1, the combustor for causing the high temperature gas B to flow through the burner flame port 3 into the filter 2A or 2B that has collected carbon in the exhaust gas E is usually a motor. A burner with a driven fan for sucking fresh air, a fuel inlet pipe, and a spark plug is used, but when incinerating the above-mentioned particulates, the temperature of the incineration air is raised from 500°C to 800°C using the burner flame or an electric heater. Since the new air is outside air, extra fuel is consumed to raise the temperature of the air itself, which increases the fuel consumption of the diesel engine as a whole.
さらに、この種排気ガス処理装置においては、
排気ガス燃焼室の後流側に熱交換器を設け燃焼用
空気を予熱して排気ガス処理装置全体の効率向上
を計ることは、例えば実公昭52−6726号のように
公知である。しかし、これらの装置においては燃
焼用空気のためのエアポンプを有しているのが普
通である。 Furthermore, in this type of exhaust gas treatment device,
It is known, for example, as disclosed in Japanese Utility Model Publication No. 52-6726, to improve the efficiency of the entire exhaust gas treatment device by providing a heat exchanger on the downstream side of the exhaust gas combustion chamber to preheat the combustion air. However, these devices usually include an air pump for combustion air.
そこで、本発明は前記従来の問題点を解消する
ためになされたものであり、デイーゼル機関の排
気ガス中の微粒子を除いてクリーンな排気ガスと
して排出させる排出ガス処理装置を提供すると共
に、その排気ガス処理装置内において捕集された
微粒子の燃焼性の向上をはかり、かつその微粒子
燃焼用の燃料の消費量の低減をはかることを目的
としたものである。 Therefore, the present invention has been made to solve the above-mentioned conventional problems, and provides an exhaust gas treatment device that removes particulates from the exhaust gas of a diesel engine and discharges it as clean exhaust gas. The purpose is to improve the combustibility of particulates collected in a gas processing device and to reduce the amount of fuel consumed for combustion of the particulates.
即ち、本発明のデイーゼル機関の排気ガス処理
装置は、デイーゼル機関の排ガス通路に微粒子捕
集用の2個のフイルタを配設すると共に、それら
2個のフイルタの一方に排気ガスを通過させなが
ら微粒子を捕集し、かつ他方で捕集した微粒子を
燃焼させる操作を交互に切換可能なデイーゼル機
関の排気ガス処理装置において、これら2個のフ
イルタの各下流側を、それぞれ出口に絞り部を有
する2分割室に形成すると共に、一方の出口から
排出される微粒子捕集後の排気ガスにより他方の
微粒子燃焼ガスを吸出す効果を有するエゼクタ効
果用可変板を、上記2分割室の出口に設け、上記
の各フイルタの各下流側の2分割室のケースを、
新規空気を予熱し、かつその加熱空気を微粒子燃
焼の燃焼器に導入可能な2重壁ケースに形成し、
更に、該燃焼器に触媒を設けることにより構成さ
れる。 That is, the diesel engine exhaust gas treatment device of the present invention includes two filters for collecting particulates disposed in the exhaust gas passage of the diesel engine, and collects particulates while passing the exhaust gas through one of the two filters. In an exhaust gas treatment device for a diesel engine that can alternately switch between collecting particulate matter and burning the collected particulates, the downstream side of each of these two filters has two filters each having a constriction part at the outlet. A variable plate for ejector effect is formed in the divided chamber and has the effect of sucking out particulate combustion gas from the other outlet by exhaust gas after collecting particulates discharged from one outlet, and is provided at the outlet of the two divided chambers, The case of the two divided chambers on the downstream side of each filter is
forming a double-walled case that can preheat fresh air and introduce the heated air into a particulate combustion combustor;
Furthermore, it is constructed by providing a catalyst in the combustor.
以下、図面を参照して本発明の実施例を説明す
るが、第1図の従来例に示す部品及び下記の各図
面に示す部品において、同じ部品は同じ部品番号
で示している。 Hereinafter, embodiments of the present invention will be described with reference to the drawings, and the same parts are indicated by the same part numbers in the parts shown in the conventional example in FIG. 1 and the parts shown in each of the drawings below.
まず、第2図に示す本発明の実施例において
は、第1図の従来例とほぼ同様にデイーゼル機関
の排気ガス通路に設けられる排気ガス処理装置を
示しており、この装置の入口に、切換弁1を介し
て排気ガスEの微粒子捕集用の2個のフイルタ2
A,2Bを配設し、その切換弁1によつて図に示
すごとく一方のフイルタ2Aに排気ガスEを通過
させながら微粒子を捕集すると共に、他方のフイ
ルタ2Aで捕集した微粒子を火炎口3からの高温
ガスBで焼却させる操作を交互に切換可能とした
排気ガス処理装置を構成している。 First, the embodiment of the present invention shown in FIG. 2 shows an exhaust gas treatment device installed in the exhaust gas passage of a diesel engine, similar to the conventional example shown in FIG. Two filters 2 for collecting particulates in the exhaust gas E via a valve 1
A and 2B are arranged, and the switching valve 1 allows the exhaust gas E to pass through one filter 2A to collect particulates as shown in the figure, and the particulates collected by the other filter 2A to be sent to the flame port. This constitutes an exhaust gas treatment device that can alternately switch between incineration operations using high-temperature gas B from three sources.
そこで本発明では、フイルタ2A,2Bの各下
流側の、第1図の従来例にて合流部4であつた部
分を仕切壁7で2分割し、かつそれぞれの出口に
絞り部を形成し、かつそれらの出口に回転軸8に
より回動可能なエゼクタ効果用可変板9を設けて
いる。 Therefore, in the present invention, the portion on the downstream side of each of the filters 2A, 2B, which was the merging portion 4 in the conventional example shown in FIG. Further, an ejector effect variable plate 9 rotatable by a rotary shaft 8 is provided at the outlet thereof.
上記の構成からなる排気ガス処理装置におい
て、フイルタ2Aで微粒子を捕集中には、このデ
イーゼル機関からの多量の排気ガスEがエゼクタ
効果用可変板9の下面を流出し、後部の排気管1
0から排出するが、この場合、エゼクタ効果用可
変板9はフイルタ2Aの通過ガス量に比例して上
部に押し上げられ、エゼクタ効果用可変板9に
て、フイルタ2Bからの微粒子を焼却した微粒子
燃焼ガスGが上記フイルタ2A通過後の排気ガス
Eにより吸出されることになる。 In the exhaust gas treatment device having the above configuration, while the filter 2A is collecting particulates, a large amount of exhaust gas E from the diesel engine flows out of the lower surface of the ejector effect variable plate 9, and the rear exhaust pipe 1
In this case, the ejector effect variable plate 9 is pushed upward in proportion to the amount of gas passing through the filter 2A, and the ejector effect variable plate 9 incinerates the particulates from the filter 2B. The gas G is sucked out by the exhaust gas E after passing through the filter 2A.
即ち、後部の排気管10等による抵抗に打ち勝
ち、フイルタ2Aからの排気ガスEが流出するこ
とによるエゼクタ効果により、フイルタ2Bの後
部室は負圧となり、バーナ燃焼に弊害を与えず、
フイルタ2A通過の排気ガス量が多い程その吸出
し効果が大となり、残留空気量を多くし、カーボ
ン粒子のフイルタ2Bでの燃焼を良好とすること
ができる。 That is, due to the ejector effect caused by overcoming the resistance from the rear exhaust pipe 10 etc. and flowing out of the exhaust gas E from the filter 2A, the rear chamber of the filter 2B becomes a negative pressure, which does not adversely affect burner combustion.
The larger the amount of exhaust gas passing through the filter 2A, the greater the suction effect, which increases the amount of residual air and improves the combustion of carbon particles in the filter 2B.
一方、フイルタ2Bをデイーゼル機関の排気ガ
スEが通過している場合には、エゼクタ効果用可
変板9は第2図の下側に押され、バランスした位
置で停止し、フイルタ2Aからの微粒子燃焼ガス
Gを吸出すことになる。 On the other hand, when the exhaust gas E of the diesel engine is passing through the filter 2B, the ejector effect variable plate 9 is pushed downward in FIG. 2 and stops at a balanced position, causing particulate combustion from the filter 2A. Gas G will be sucked out.
なお、上記実施例では回転軸8に対して、エゼ
クタ効果用可変板9を回動自由に取り付け、フイ
ルタ2A、または2Bからの排気ガスEの流れに
より移動するようにしているが、この回転軸8の
外部にレバーを取り付け、そのレバーの先端を2
個のばね等により中立位置にバランスさせても良
く、また、そのレバー回動角度を各フイルタ2
A,2Bの後部室からの圧力に連動して作動する
可変ピストン等を介して自動調整させても良い。 In the above embodiment, the ejector effect variable plate 9 is rotatably attached to the rotating shaft 8 and is moved by the flow of exhaust gas E from the filter 2A or 2B. Attach a lever to the outside of 8, and attach the tip of the lever to 2.
It is also possible to balance the lever to a neutral position using a spring or the like, and the rotation angle of the lever may be adjusted to
It may be automatically adjusted via a variable piston or the like that operates in conjunction with the pressure from the rear chambers A and 2B.
次に、第2図に示すごとく、フイルタ2A,2
Bの各下流側の2分割室のケースを2重壁ケース
16に形成し、この2重壁ケース16の壁間に新
規空気Aを導入して排気ガスE及び微粒子燃焼ガ
スGで予熱し、その加熱空気Ahを、第3図に示
す側断面図及び第4図に示す平面図のごとく微粒
子焼却用の燃焼器15へ導入するように空気配管
11が設けられている。 Next, as shown in FIG.
A double wall case 16 is formed as a case for each of the two downstream divided chambers of B, and new air A is introduced between the walls of this double wall case 16 and preheated with exhaust gas E and particulate combustion gas G, An air pipe 11 is provided so as to introduce the heated air Ah into a combustor 15 for particulate incineration, as shown in the side sectional view shown in FIG. 3 and the plan view shown in FIG. 4.
この燃焼器15には、一次点火栓14、燃料を
噴射する燃料弁13及び触媒12が設けられ、燃
料弁13からの燃料噴射と一次点火栓14の点火
とにより2重壁ケース16で予熱された加熱空気
Ahを用いての触媒燃焼による微粒子焼却用火炎
を焼却火炎切換弁17を介してフイルタ2Aまた
は2Bへ供給するようになつている。 This combustor 15 is provided with a primary ignition plug 14, a fuel valve 13 for injecting fuel, and a catalyst 12, and is preheated in a double-walled case 16 by fuel injection from the fuel valve 13 and ignition of the primary ignition plug 14. heated air
A particulate incineration flame resulting from catalytic combustion using Ah is supplied to the filter 2A or 2B via an incineration flame switching valve 17.
その結果、予熱された加熱空気Ahの空気流動
中にて一次点火した後、触媒12による連続燃焼
により過剰空気を含んだ高温ガスBをフイルタ2
A、または2B中に供給して、カーボンなどの微
粒子を焼却することができる。 As a result, after the preheated heated air Ah is primarily ignited during the air flow, the high temperature gas B containing excess air is transferred to the filter 2 through continuous combustion by the catalyst 12.
A or 2B can be supplied to incinerate fine particles such as carbon.
従つて、本発明の排気ガス処理装置を適用した
デイーゼル機関では、2個のフイルタを交互に使
用して排気ガス処理を行なう際、一方のフイルタ
から排出される排気ガス中の微粒子燃焼ガスが他
方のフイルタからの排気ガスのエゼクタ効果によ
り吸出され、微粒子の燃焼を良好にするので、フ
イルタの目づまりも少なくなり、その結果、出力
を良好に維持すると共に、排気ガスの清浄効果を
維持することができる。 Therefore, in a diesel engine to which the exhaust gas treatment device of the present invention is applied, when two filters are used alternately to perform exhaust gas treatment, particulate combustion gas in the exhaust gas discharged from one filter is mixed with the other filter. The exhaust gas from the filter is sucked out by the ejector effect, and the combustion of particulates is improved, so the filter is less clogged, and as a result, the output is maintained at a good level, and the exhaust gas cleaning effect is maintained. I can do it.
特に、本発明では、微粒子燃焼用の燃焼器に触
媒を設けると共に、2重壁ケースから予熱された
新規空気をこの燃焼器に導入するので一度触媒燃
焼が開始されると、その連続反応により燃焼され
ることになり、従来のバーナ燃焼器に比較して空
燃比の使用範囲が拡大され、燃焼器自身によるカ
ーボン発生などを生じない過剰空気状態のクリー
ンな燃焼ガスが得られるという利点がある。 In particular, in the present invention, a catalyst is provided in the combustor for particulate combustion, and new preheated air is introduced into the combustor from the double-walled case, so once catalytic combustion has started, the continuous reaction causes combustion. Compared to conventional burner combustors, the range of air-fuel ratios that can be used is expanded, and the combustor itself has the advantage of producing clean combustion gas with excess air that does not generate carbon.
また、2重壁ケースから予熱された新規空気を
燃焼器に導入するので、燃焼器に使用する燃料消
費量の低減およびフイルタの燃焼時の過剰空気温
度の上昇が得られ、捕集された微粒子の燃焼時間
が大幅に短縮される。 In addition, since preheated fresh air is introduced into the combustor from the double-walled case, the amount of fuel used in the combustor is reduced and the temperature of excess air during combustion of the filter is increased. combustion time is significantly reduced.
従つて、微粒子の燃焼が短時間に可能となるた
め、デイーゼル機関からの排気ガス中の微粒子捕
集用フイルタのサイズを小形化し、短時間にフイ
ルタの切換実施が可能となり、高値なフイルタの
小形化による低コスト化、装置の小形化、低コス
ト化が得られるという利点もある。 Therefore, it is possible to burn particulates in a short period of time, making it possible to reduce the size of the filter for collecting particulates in the exhaust gas from a diesel engine, and to change the filter in a short period of time, thereby reducing the size of expensive filters. It also has the advantage of being able to reduce costs by reducing the size of the device, making the device more compact, and lowering costs.
第1図は従来のデイーゼル機関の排気ガス処理
装置の平断面図、第2図は本考案の実施例におけ
るデイーゼル機関の排気ガス処理装置の平断面
図、第3図は第2図の側断面図、第4図は第2図
の平面図である。
1…切換弁、2A,2B…フイルタ、3…火炎
口、6…仕切壁、7…仕切壁、8…回転軸、9…
エゼクタ効果用可変板、11…空気配管、12…
触媒、14…一次点火栓、15…燃焼器、16…
2重壁ケース、E…排気ガス、G…微粒子燃焼ガ
ス、A…新規空気。
FIG. 1 is a plan sectional view of a conventional exhaust gas treatment device for a diesel engine, FIG. 2 is a plan sectional view of an exhaust gas treatment device for a diesel engine according to an embodiment of the present invention, and FIG. 3 is a side sectional view of FIG. 2. FIG. 4 is a plan view of FIG. 2. DESCRIPTION OF SYMBOLS 1...Switching valve, 2A, 2B...Filter, 3...Flare port, 6...Partition wall, 7...Partition wall, 8...Rotating shaft, 9...
Variable plate for ejector effect, 11...Air piping, 12...
Catalyst, 14...Primary ignition plug, 15...Combustor, 16...
Double wall case, E...Exhaust gas, G...Particulate combustion gas, A...New air.
Claims (1)
の2個のフイルタを配設すると共に、それら2個
のフイルタの一方に排気ガスを通過させながら微
粒子を捕集し、かつ他方で捕集した微粒子を燃焼
させる操作を交互に切換可能なデイーゼル機関の
排気ガス処理装置において、これら2個のフイル
タの各下流側を、それぞれ出口に絞り部を有する
2分割室に形成すると共に、一方の出口から排出
される微粒子捕集後の排気ガスにより他方の微粒
子燃焼ガスを吸出す効果を有するエゼクタ効果用
可変板を、該2分割室の出口に設け、上記の各フ
イルタの各下流側の2分割室のケースを、新規空
気を予熱し、かつその加熱空気を微粒子燃焼の燃
焼器に導入可能な2重壁ケースに形成し、更に、
該燃焼器に触媒を設けたことを特徴とするデイー
ゼル機関の排気ガス処理装置。1. Two filters for collecting particulates are arranged in the exhaust gas passage of a diesel engine, and particulates are collected while passing the exhaust gas through one of the two filters, and the particulates collected by the other filter are collected. In an exhaust gas treatment device for a diesel engine that can alternately switch the combustion operation, each of the downstream sides of these two filters is formed into two divided chambers each having a constriction part at the outlet, and the exhaust gas is discharged from one outlet. A variable plate for ejector effect having the effect of sucking out the other particulate combustion gas by the exhaust gas after collecting particulates is provided at the outlet of the two divided chambers, and the case of each of the two divided chambers on the downstream side of each of the filters is is formed into a double-walled case capable of preheating fresh air and introducing the heated air into a combustor for particulate combustion;
An exhaust gas treatment device for a diesel engine, characterized in that the combustor is provided with a catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57210575A JPS59101522A (en) | 1982-12-02 | 1982-12-02 | Exhaust gas treating device for diesel engine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57210575A JPS59101522A (en) | 1982-12-02 | 1982-12-02 | Exhaust gas treating device for diesel engine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59101522A JPS59101522A (en) | 1984-06-12 |
| JPS6361489B2 true JPS6361489B2 (en) | 1988-11-29 |
Family
ID=16591580
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57210575A Granted JPS59101522A (en) | 1982-12-02 | 1982-12-02 | Exhaust gas treating device for diesel engine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59101522A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0354879U (en) * | 1989-09-30 | 1991-05-27 | ||
| JPH0354877U (en) * | 1989-09-28 | 1991-05-27 |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0517370Y2 (en) * | 1986-12-26 | 1993-05-11 | ||
| JPH01134715U (en) * | 1988-03-09 | 1989-09-14 | ||
| US5212948A (en) * | 1990-09-27 | 1993-05-25 | Donaldson Company, Inc. | Trap apparatus with bypass |
| DE4405045C2 (en) * | 1994-02-17 | 1998-04-09 | Eberspaecher J Gmbh & Co | Device for the thermal aftertreatment of the engine exhaust gas and its use |
| FR2879654B1 (en) * | 2004-12-20 | 2010-04-30 | Inst Francais Du Petrole | METHOD FOR REGENERATING PARTICLE FILTER WITH CATALYTIC COMBUSTION DEVICE AND FILTRATION FACILITY USING SUCH A METHOD |
| DK2198132T3 (en) * | 2007-08-30 | 2011-07-11 | Energy Conversion Technology As | Exhaust gas apparatus and method for regenerating a NOx separator and a particulate filter |
| JP5849178B2 (en) * | 2009-12-17 | 2016-01-27 | パナソニックIpマネジメント株式会社 | Exhaust gas purification device |
| WO2011043046A1 (en) * | 2009-10-06 | 2011-04-14 | パナソニック株式会社 | Exhaust gas purification device |
| GB2510171B (en) | 2013-01-28 | 2015-01-28 | Cool Flame Technologies As | Method and cleaning apparatus for removal of SOx and NOx from exhaust gas |
-
1982
- 1982-12-02 JP JP57210575A patent/JPS59101522A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0354877U (en) * | 1989-09-28 | 1991-05-27 | ||
| JPH0354879U (en) * | 1989-09-30 | 1991-05-27 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59101522A (en) | 1984-06-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4167852A (en) | Diesel engine exhaust cleaner and burner | |
| US5251564A (en) | Combustion box exhaust filtration system and method | |
| US4651524A (en) | Exhaust processor | |
| US4730455A (en) | Process and system for the regeneration of particulate filter traps | |
| CN102080587A (en) | Regenerating unit and method of diesel particle trap | |
| JPS6361489B2 (en) | ||
| CN110778378B (en) | A DPF hot air regeneration reduction system and control method | |
| JPS6361488B2 (en) | ||
| CN110273731A (en) | A kind of burner meeting grain catcher DPF worst cold case highly efficient regeneration | |
| JP2001073743A (en) | Exhaust purifying device for diesel engine | |
| JP2003035130A (en) | Regeneration method of soot-reducing device, and regenerating device using the same | |
| JPS5977022A (en) | Exhaust gas purifier for diesel engine | |
| CN210948849U (en) | DPF hot air regeneration and reduction system | |
| JPH024106A (en) | Deodorization incinerator | |
| JP2888160B2 (en) | High frequency exhaust gas purification equipment | |
| JPS5820918A (en) | Purifier of exhaust gas | |
| JP2000110548A (en) | Black smoke removal device | |
| JPS5929718A (en) | Regenerating burner for particulate filter | |
| JPS6141937Y2 (en) | ||
| CN223106059U (en) | A hot air furnace with waste gas incineration structure | |
| JPS56132416A (en) | Device for disposing of exhaust gas of diesel engine | |
| JPS6329135Y2 (en) | ||
| JP2562787B2 (en) | Exhaust gas cleaning device | |
| CN216244292U (en) | Solid waste incinerator | |
| JPH0540250Y2 (en) |