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JP2006161768A - Exhaust purification device - Google Patents

Exhaust purification device Download PDF

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JP2006161768A
JP2006161768A JP2004357732A JP2004357732A JP2006161768A JP 2006161768 A JP2006161768 A JP 2006161768A JP 2004357732 A JP2004357732 A JP 2004357732A JP 2004357732 A JP2004357732 A JP 2004357732A JP 2006161768 A JP2006161768 A JP 2006161768A
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fuel
nox
exhaust
fuel reforming
plasma
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Masatoshi Shimoda
正敏 下田
Yoshihide Takenaka
嘉英 竹中
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Hino Motors Ltd
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Hino Motors Ltd
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Priority to JP2004357732A priority Critical patent/JP2006161768A/en
Priority to US11/721,057 priority patent/US7913486B2/en
Priority to PCT/JP2005/022448 priority patent/WO2006062124A1/en
Priority to DE602005015897T priority patent/DE602005015897D1/en
Priority to EP05814697A priority patent/EP1835137B1/en
Publication of JP2006161768A publication Critical patent/JP2006161768A/en
Pending legal-status Critical Current

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Abstract

【課題】運転条件にかかわらず常に高いNOx低減率を得られるようにした排気浄化装置を提供する。
【解決手段】排気流路2,4の途中にNOx吸蔵還元触媒5を装備してNOxを還元浄化するように構成した排気浄化装置であって、排気流路2,4におけるNOx吸蔵還元触媒5の上流側に、燃料をH2とCOに分解する燃料改質触媒構造7又はプラズマ燃料改質手段を設ける。
【選択図】図1
An exhaust emission control device capable of always obtaining a high NOx reduction rate regardless of operating conditions is provided.
An exhaust gas purification apparatus configured to reduce and purify NOx by providing a NOx occlusion reduction catalyst 5 in the middle of exhaust flow paths 2 and 4, wherein the NOx occlusion reduction catalyst 5 in the exhaust flow paths 2 and 4 is provided. Is provided with a fuel reforming catalyst structure 7 or plasma fuel reforming means for decomposing the fuel into H 2 and CO.
[Selection] Figure 1

Description

本発明は、排気浄化装置に関するものである。   The present invention relates to an exhaust emission control device.

従来より、排気管の途中に装備した排気浄化用触媒により排気浄化を図ることが行われており、この種の排気浄化用触媒としては、排気燃料比がリーンの時に排気ガス中のNOxを酸化して硝酸塩の状態で一時的に吸蔵し、排気ガス中のO2濃度が低下した時に未燃HCやCO等の介在によりNOxを分解放出して還元浄化する性質を備えたNOx吸蔵還元触媒が知られている。 Conventionally, exhaust purification is performed with an exhaust purification catalyst installed in the middle of the exhaust pipe. This type of exhaust purification catalyst oxidizes NOx in exhaust gas when the exhaust fuel ratio is lean. Thus, a NOx occlusion reduction catalyst having the property of temporarily storing in the form of nitrate and decomposing and releasing NOx through the intervention of unburned HC, CO, etc. when the O 2 concentration in the exhaust gas decreases is reduced and purified. Are known.

この種のNOx吸蔵還元触媒としては、白金・バリウム・アルミナ触媒や、白金・カリウム・アルミナ触媒等が前述した如き性質を有するものとして既に知られている。   As this type of NOx occlusion reduction catalyst, platinum / barium / alumina catalyst, platinum / potassium / alumina catalyst, and the like have already been known.

そして、NOx吸蔵還元触媒においては、NOxの吸蔵量が増大して飽和量に達してしまうと、それ以上のNOxを吸蔵できなくなるため、定期的にNOx吸蔵還元触媒に流入する排気ガスのO2濃度を低下させてNOxを分解放出させる必要がある。 In the NOx occlusion reduction catalyst, when the occlusion amount of NOx increases and reaches the saturation amount, no more NOx can be occluded, and therefore, O 2 of the exhaust gas flowing into the NOx occlusion reduction catalyst periodically. It is necessary to decompose and release NOx by reducing the concentration.

例えば、ガソリン機関に使用した場合であれば、機関の運転空燃比を低下(空燃比が燃料リッチ時で機関を運転)することにより、排気ガス中のO2濃度を低下し且つ排気ガス中の未燃HCやCO等の還元成分を増加してNOxの分解放出を促すことができるが、NOx吸蔵還元触媒をディーゼル機関の排気浄化装置として使用した場合には、空燃比が燃料リッチ時で機関を運転することが困難である。 For example, when used in a gasoline engine, by reducing the operating air-fuel ratio of the engine (operating the engine when the air-fuel ratio is rich in fuel), the O 2 concentration in the exhaust gas is reduced and the exhaust gas in the exhaust gas Although it is possible to promote the decomposition and release of NOx by increasing the reducing components such as unburned HC and CO, when the NOx storage reduction catalyst is used as an exhaust gas purification device for a diesel engine, the air-fuel ratio is high when the fuel is rich. Is difficult to drive.

このため、NOx吸蔵還元触媒の上流側で排気ガス中に燃料(HC)を添加することにより、この添加燃料を還元剤としてNOx吸蔵還元触媒上でO2と反応させることで排気ガス中のO2濃度を低下させる必要がある(例えば、特許文献1参照)。
特開2000−356127号公報
For this reason, by adding fuel (HC) to the exhaust gas upstream of the NOx storage reduction catalyst, the added fuel is used as a reducing agent to react with O 2 on the NOx storage reduction catalyst. 2 It is necessary to reduce the concentration (see, for example, Patent Document 1).
JP 2000-356127 A

しかしながら、このようにNOx吸蔵還元触媒の上流側で燃料添加を行う方式では、その添加燃料が蒸発して生じたHCの一部がNOx吸蔵還元触媒の表面上で排気ガス中のO2と反応(燃焼)し、NOx吸蔵還元触媒の周囲の雰囲気中におけるO2濃度がほぼ零となってからNOxの分解放出が開始されることになるため、NOx吸蔵還元触媒の表面上でHCがO2と反応(燃焼)するのに必要な燃焼温度(約220〜250℃)が得られない運転条件下(例えば渋滞の多い都市内での徐行運転等)では、NOx吸蔵還元触媒からNOxを効率良く分解放出させることができず、NOx吸蔵還元触媒の再生が効率良く進まないことで触媒の容積中に占めるNOx吸蔵サイトの回復割合が小さくなって吸蔵能力が落ちるという問題があった。 However, in the method of adding fuel upstream of the NOx storage reduction catalyst in this way, a part of HC generated by evaporation of the added fuel reacts with O 2 in the exhaust gas on the surface of the NOx storage reduction catalyst. (Combustion), and NOx decomposition and release is started after the O 2 concentration in the atmosphere around the NOx storage reduction catalyst becomes almost zero, so that HC is O 2 on the surface of the NOx storage reduction catalyst. NOx is efficiently removed from the NOx occlusion reduction catalyst under operating conditions where the combustion temperature (about 220-250 ° C) required for reaction (combustion) with NOx cannot be obtained (for example, slow driving in cities with heavy traffic). There was a problem that the NOx occlusion reduction catalyst could not be decomposed and released, and the regeneration of the NOx occlusion reduction catalyst did not proceed efficiently, so that the recovery rate of the NOx occlusion site in the catalyst volume was reduced and the occlusion capacity was lowered.

本発明は上述の実情に鑑みてなしたもので、運転条件にかかわらず常に高いNOx低減率を得られるようにした排気浄化装置を提供することを目的としている。   The present invention has been made in view of the above circumstances, and an object of the present invention is to provide an exhaust emission control device that can always obtain a high NOx reduction rate regardless of operating conditions.

本発明は、排気流路の途中にNOx吸蔵還元触媒を装備してNOxを還元浄化するように構成した排気浄化装置であって、前記排気流路におけるNOx吸蔵還元触媒の上流側に、燃料をH2とCOに分解する燃料改質触媒構造又はプラズマ燃料改質手段を設けたことを特徴とする排気浄化装置、に係るものである。 The present invention is an exhaust emission control device configured to reduce and purify NOx by installing a NOx storage reduction catalyst in the middle of an exhaust flow path, wherein fuel is supplied to the upstream side of the NOx storage reduction catalyst in the exhaust flow path. The present invention relates to an exhaust emission control device provided with a fuel reforming catalyst structure or plasma fuel reforming means that decomposes into H 2 and CO.

本発明は、排気流路における燃料改質触媒構造又はプラズマ燃料改質手段の上流側に、NOをNO2に酸化するプラズマ発生手段を配置しても良い。 In the present invention, a plasma generating means for oxidizing NO into NO 2 may be disposed upstream of the fuel reforming catalyst structure or the plasma fuel reforming means in the exhaust passage.

本発明において、プラズマ発生手段は、排気燃料比がリーン時にNOをNO2に酸化してNOx吸蔵還元触媒によるNOx吸蔵を促進させるよう制御されても良い。 In the present invention, the plasma generating means may be controlled to oxidize NO to NO 2 when the exhaust fuel ratio is lean to promote NOx occlusion by the NOx occlusion reduction catalyst.

本発明において、燃料改質触媒構造又はプラズマ燃料改質手段は、空燃比が燃料リッチ時に燃料をH2とCOに分解してNOx吸蔵還元触媒のNOxを還元するよう制御されても良い。 In the present invention, the fuel reforming catalyst structure or the plasma fuel reforming means may be controlled to reduce the NOx of the NOx occlusion reduction catalyst by decomposing the fuel into H 2 and CO when the air-fuel ratio is rich in fuel.

本発明において、燃料改質触媒構造又はプラズマ燃料改質手段は、排気温度が充分高い場合には燃料を非分解で供給して瞬間的に燃料を濃くするよう制御されても良い。   In the present invention, the fuel reforming catalyst structure or the plasma fuel reforming means may be controlled such that when the exhaust temperature is sufficiently high, the fuel is supplied without being decomposed and the fuel is instantly concentrated.

而して、このように本発明によれば、燃料改質触媒構造又はプラズマ燃料改質手段によりH2とCOに分解し得るので、H2及びCOによりNOx吸蔵還元触媒の表面上のNOxを効率良くN2に還元処理し、結果的に、様々な運転条件にかかわらず常に高いNOx低減率を得ることができる。又、燃料を、燃料改質触媒構造又はプラズマ燃料改質手段にてH2とCOに分解させ、反応性の高いH2及びCOにより比較的低い温度領域から高いNOx低減率を得ることができるので、例えば渋滞の多い都市内での徐行運転等のように低負荷で排気温度が低い運転状態が継続され易い運転条件下であっても、車外に排出される排気ガス中に含まれるNOxを従来より効果的に低減することができる。 Thus, according to the present invention, since it can be decomposed into H 2 and CO by the fuel reforming catalyst structure or the plasma fuel reforming means, NO x on the surface of the NO x storage reduction catalyst is converted by H 2 and CO. efficiently reducing treatment in N 2, as a result, it is possible to obtain a very high NOx reduction ratio irrespective of the various operating conditions. Further, fuel, by the fuel reforming catalyst structure or a plasma fuel reformer unit is decomposed into H 2 and CO, it is possible to obtain a high NOx reduction rate from a relatively low temperature region by highly reactive H 2 and CO Therefore, NOx contained in the exhaust gas exhausted outside the vehicle can be maintained even under operating conditions in which low-exhaust and low-exhaust temperature operating conditions are likely to continue, such as slow driving in cities with heavy traffic. This can be reduced more effectively than before.

本発明は、排気流路における燃料改質触媒構造又はプラズマ燃料改質手段の上流側に、NOをNO2に酸化するプラズマ発生手段を配置すると、プラズマ発生手段により温度に関係なくNOをNO2に酸化し得るので、NOx吸蔵還元触媒によるNOx吸蔵を容易にすることができる。 According to the present invention, when a plasma generating means for oxidizing NO into NO 2 is disposed upstream of the fuel reforming catalyst structure or the plasma fuel reforming means in the exhaust passage, the plasma generating means converts NO to NO 2 regardless of the temperature. Therefore, NOx occlusion by the NOx occlusion reduction catalyst can be facilitated.

本発明において、プラズマ発生手段は、排気燃料比がリーン時にNOをNO2に酸化してNOx吸蔵還元触媒によるNOx吸蔵を促進させるよう制御されると、NOx吸蔵還元触媒によるNOx吸蔵を一層容易にすることができる。 In the present invention, a plasma generating means, the exhaust fuel ratio is controlled so as to promote the NOx occlusion by oxidation to NOx storage reduction catalyst of NO to NO 2 in the lean, the NOx storage by the NOx storage reduction catalyst more readily can do.

本発明において、燃料改質触媒構造又はプラズマ燃料改質手段は、空燃比が燃料リッチ時に燃料をH2とCOに分解してNOx吸蔵還元触媒のNOxを還元するよう制御されると、H2及びCOによりNOx吸蔵還元触媒の表面上のNOxを一層効率良くN2に還元処理することができる。 In the present invention, the fuel reforming catalyst structure or a plasma fuel reformer unit, the air-fuel ratio is controlled so that the fuel is decomposed into H 2 and CO reducing NOx of the NOx storage reduction catalyst during the fuel-rich, H 2 Further, NOx on the surface of the NOx storage reduction catalyst can be more efficiently reduced to N 2 by CO and CO.

本発明において、燃料改質触媒構造又はプラズマ燃料改質手段は、排気温度が充分高い場合には燃料を非分解で供給して瞬間的に燃料を濃くするよう制御されると、NOx吸蔵還元触媒の表面上のNOxを適切にN2に還元処理することができる。 In the present invention, when the fuel reforming catalyst structure or the plasma fuel reforming means is controlled so that the fuel is supplied without being decomposed and the fuel is instantly concentrated when the exhaust temperature is sufficiently high, the NOx occlusion reduction catalyst NOx on the surface can be reduced to N 2 appropriately.

上記した本発明の排気浄化装置によれば、温度に関係なく、NOをNO2に酸化し、もしくは燃料をH2とCOに分解し得るので、常に高いNOx低減率を得ることができるというの優れた効果を奏し得る。 According to the above-described exhaust purification apparatus of the present invention, NO can be oxidized to NO 2 or the fuel can be decomposed into H 2 and CO regardless of the temperature, so that a high NOx reduction rate can always be obtained. An excellent effect can be achieved.

以下本発明の実施の形態を図面を参照しつつ説明する。   Embodiments of the present invention will be described below with reference to the drawings.

図1〜図4は本発明をNOx吸蔵還元触媒を用いて実施する形態の一例であって、ディーゼルエンジン1から排気マニホールド2を介して排出される排気ガス3が流通する排気管4の途中に、フロースルー方式のハニカム構造を有するNOx吸蔵還元触媒5をケーシング6に抱持させて装備している。   1 to 4 show an example of an embodiment in which the present invention is implemented using a NOx occlusion reduction catalyst. In the middle of an exhaust pipe 4 through which exhaust gas 3 discharged from a diesel engine 1 through an exhaust manifold 2 flows. The NOx occlusion reduction catalyst 5 having a flow-through type honeycomb structure is mounted on the casing 6.

排気管4におけるケーシング6より上流側には、燃料改質触媒構造7又はプラズマ燃料改質手段8を設けている。   A fuel reforming catalyst structure 7 or plasma fuel reforming means 8 is provided upstream of the casing 6 in the exhaust pipe 4.

ここで、燃料改質触媒構造7の好適な一例を示すと、図1、図3に示す如く、燃料改質触媒構造7は、排気管4へ通じる導入管9と排出管10を備えて内部空間11を形成する燃料改質器12と、燃料改質器12内に設置される燃料改質触媒13と、燃料改質器12の内部空間11へ上流側から燃料を添加する燃料添加ノズル14と、導入管9を開閉する導入バルブ15と、排出管10を開閉する排出バルブ16とを備えている。   Here, a preferred example of the fuel reforming catalyst structure 7 is shown. As shown in FIGS. 1 and 3, the fuel reforming catalyst structure 7 includes an introduction pipe 9 and an exhaust pipe 10 that communicate with the exhaust pipe 4 and has an internal structure. A fuel reformer 12 that forms the space 11, a fuel reforming catalyst 13 installed in the fuel reformer 12, and a fuel addition nozzle 14 that adds fuel from the upstream side to the internal space 11 of the fuel reformer 12. And an introduction valve 15 for opening and closing the introduction pipe 9 and a discharge valve 16 for opening and closing the discharge pipe 10.

一方、プラズマ燃料改質手段8の好適な一例を示すと、図2、図4に示す如く、プラズマ燃料改質手段8は、排気管4に通じるプラズマ燃料改質器17と、プラズマ燃料改質器17に電圧を印加する高圧電源18とを備えており、プラズマ燃料改質器17は、排気管4へ通じる内部空間19を形成すると共に接地電極となる排出部20と、排出部20の内部空間19へ軽油等の燃料と空気の燃料混合ガスを導くよう混合ガス流路21を形成する導入部22と、排出部20と導入部22の間に配置される絶縁体部23と、導入部22に支持される高電圧電極24とを備えている。尚、図中、25は排出部20を冷却する冷却水流路、26は排出部20と導入部22を固定する固定ボルトを示している。又、排出部20は、高電圧電極24側の端部20aを接地電極とせずに絶縁体にしても良い。   On the other hand, as a preferred example of the plasma fuel reforming means 8, as shown in FIGS. 2 and 4, the plasma fuel reforming means 8 includes a plasma fuel reformer 17 communicating with the exhaust pipe 4, and a plasma fuel reforming. The plasma fuel reformer 17 forms an internal space 19 that leads to the exhaust pipe 4 and serves as a ground electrode, and an internal portion of the exhaust unit 20. An introduction portion 22 that forms a mixed gas flow path 21 so as to guide a fuel mixed gas of fuel such as light oil and air to the space 19, an insulator portion 23 disposed between the discharge portion 20 and the introduction portion 22, and an introduction portion 22 and a high voltage electrode 24 supported by 22. In the figure, reference numeral 25 denotes a cooling water flow path for cooling the discharge part 20, and 26 denotes a fixing bolt for fixing the discharge part 20 and the introduction part 22. Further, the discharge portion 20 may be an insulator without using the end portion 20a on the high voltage electrode 24 side as a ground electrode.

排気管4における燃料改質触媒構造7又はプラズマ燃料改質手段8の上流側には、図1、図2に示す如く、排気管4内で対向配置された対の平板電極からなるプラズマ発生器27と、プラズマ発生器27に電圧を印加する高圧電源28とを備えたプラズマ発生手段29を設けている。   On the upstream side of the fuel reforming catalyst structure 7 or the plasma fuel reforming means 8 in the exhaust pipe 4, as shown in FIGS. 1 and 2, a plasma generator comprising a pair of flat plate electrodes arranged opposite to each other in the exhaust pipe 4. 27 and a plasma generating means 29 including a high voltage power source 28 for applying a voltage to the plasma generator 27 is provided.

そして、ディーゼルエンジン1には、その機関回転数を検出する回転センサ30が装備されており、回転センサ30からの回転数信号30aと、アクセルセンサ31(アクセルペダルの踏み込み角度を検出するセンサ)からの負荷信号31aと、排気管4に設置された温度センサ32からの温度信号32aが制御装置33に入力されるようになっている。   The diesel engine 1 is equipped with a rotation sensor 30 that detects the engine speed, and from a rotation speed signal 30a from the rotation sensor 30 and an accelerator sensor 31 (a sensor that detects the depression angle of the accelerator pedal). Load signal 31 a and a temperature signal 32 a from a temperature sensor 32 installed in the exhaust pipe 4 are input to the control device 33.

一方、制御装置33においては、前述した回転センサ30からの回転数信号30aと、アクセルセンサ31からの負荷信号31aとから判断される現在の運転状態に基づきNOxの発生量等が推定されると共に、その推定されたNOxの発生量と、温度センサ32からの温度信号32a等から燃料改質触媒構造7又はプラズマ燃料改質手段8、及びプラズマ発生手段29を制御するようになっている。ここで、制御装置33は、他のセンサから信号を受けて、燃料改質触媒構造7又はプラズマ燃料改質手段8、及びプラズマ発生手段29を制御するようにしても良い。   On the other hand, in the control device 33, the amount of NOx generated and the like are estimated based on the current operating state determined from the rotation speed signal 30a from the rotation sensor 30 and the load signal 31a from the accelerator sensor 31. The fuel reforming catalyst structure 7 or the plasma fuel reforming means 8 and the plasma generating means 29 are controlled from the estimated NOx generation amount, the temperature signal 32a from the temperature sensor 32, and the like. Here, the control device 33 may control the fuel reforming catalyst structure 7 or the plasma fuel reforming means 8 and the plasma generating means 29 in response to a signal from another sensor.

尚、図1、図2中における34はターボチャージャ、35は吸気管、36はインタークーラを示す。   In FIGS. 1 and 2, reference numeral 34 denotes a turbocharger, 35 denotes an intake pipe, and 36 denotes an intercooler.

以下、本発明の実施の形態例の作用を説明する。   The operation of the embodiment of the present invention will be described below.

種々の運転状態において回転センサ30及びアクセルセンサ31からNOxの発生量等を推定すると共に温度センサ32で温度を検出した際には、制御装置(制御手段)33により適宜プラズマ発生手段29に制御信号28aを送ってプラズマ発生手段29を制御すると共に、燃料改質触媒構造7の場合には制御装置(制御手段)33により燃料改質触媒構造7に制御信号9a,10aを送って燃料添加ノズル14の添加量、導入バルブ15及び排出バルブ16の開閉を制御し、一方、プラズマ燃料改質手段8の場合には制御装置(制御手段)33によりプラズマ燃料改質手段8に制御信号18aを送って燃料の添加量及び高圧電源18の供給を制御する。   In various operating states, when the amount of NOx generated from the rotation sensor 30 and the accelerator sensor 31 is estimated and the temperature sensor 32 detects the temperature, the control device (control means) 33 controls the plasma generation means 29 appropriately. 28a is sent to control the plasma generating means 29, and in the case of the fuel reforming catalyst structure 7, the control device (control means) 33 sends control signals 9a and 10a to the fuel reforming catalyst structure 7 to send the fuel addition nozzle 14 In the case of the plasma fuel reforming means 8, the control device (control means) 33 sends a control signal 18a to the plasma fuel reforming means 8 in the case of the plasma fuel reforming means 8. The amount of fuel added and the supply of the high voltage power source 18 are controlled.

次いで、プラズマ発生手段29では、高圧電源28により平板電極のプラズマ発生器27に高電圧を印加して排気管4内にプラズマを発生させ、温度に影響を受けることなく、排気ガス3中のNOをNO2に酸化する。 Next, in the plasma generating means 29, a high voltage is applied to the flat plate plasma generator 27 by the high voltage power source 28 to generate plasma in the exhaust pipe 4, and the NO in the exhaust gas 3 is not affected by the temperature. Is oxidized to NO 2 .

又、燃料改質触媒構造7は、燃料改質器12へ供給する燃料添加量を制御すると共に温度をコントロールし、燃料改質触媒13により生じるH2とCOの発生を制御して排気ガス3中へ供給する。一方、プラズマ燃料改質手段8は、高圧電源18により高電圧電極24に高電圧を印加することによってバリア放電により内部空間19へプラズマを発生させ、温度に影響を受けることなく、内部空間19で燃料をH2とCOに改質し、改質ガス(水素混合ガス)を排気ガス3中へ供給する。 The fuel reforming catalyst structure 7 controls the amount of fuel added to the fuel reformer 12 and the temperature, and controls the generation of H 2 and CO generated by the fuel reforming catalyst 13 to control the exhaust gas 3. Supply inside. On the other hand, the plasma fuel reforming means 8 generates a plasma in the internal space 19 by barrier discharge by applying a high voltage to the high voltage electrode 24 from the high voltage power source 18 and is not affected by the temperature in the internal space 19. The fuel is reformed into H 2 and CO, and a reformed gas (hydrogen mixed gas) is supplied into the exhaust gas 3.

ここで、排気燃料比がリーン時には、制御装置33からの制御信号28aによりプラズマ発生手段29を作動させ、NOをNO2に酸化してNOx吸蔵還元触媒5によるNOx吸蔵を促進させており、又、NOxを還元する場合の空燃比が燃料リッチ時には、制御装置33からの制御信号9a,10a,18aにより燃料改質触媒構造7又はプラズマ燃料改質手段8を作動させ、燃料をH2とCOに分解して排気ガス3中へ供給し、NOx吸蔵還元触媒5に吸蔵されたNOxを効率的に還元させている。 Here, at the time of the exhaust fuel ratio lean, activates the plasma generating means 29 by the control signal 28a from the controller 33, and to promote NOx storage by the NOx storage reduction catalyst 5 oxidizes NO to NO 2, The When the air-fuel ratio when reducing NOx is rich in fuel, the fuel reforming catalyst structure 7 or the plasma fuel reforming means 8 is operated by the control signals 9a, 10a, and 18a from the control device 33, and the fuel is H 2 and CO 2. The NOx occluded by the NOx occlusion reduction catalyst 5 is efficiently reduced by being decomposed into the exhaust gas 3 and supplied into the exhaust gas 3.

更に、排気温度が充分高い場合(350℃以上)には、制御装置33により、燃料改質触媒構造7の燃料改質触媒13で処理することなく、又はプラズマ燃料改質手段8の高電圧電極24へ高電圧を印加することなく、燃料を流下して非分解で供給し、リッチスパイクとして瞬間的に燃料を濃くし、NOx吸蔵還元触媒5に吸蔵されたNOxを還元させても良い。   Further, when the exhaust temperature is sufficiently high (350 ° C. or higher), the control device 33 does not process the fuel reforming catalyst 13 of the fuel reforming catalyst structure 7 or the high voltage electrode of the plasma fuel reforming means 8. Without applying a high voltage to 24, the fuel may flow down and supplied without decomposition, and the fuel may be enriched instantaneously as a rich spike, and NOx occluded in the NOx occlusion reduction catalyst 5 may be reduced.

而して、本発明の実施の形態によれば、燃料改質触媒構造7又はプラズマ燃料改質手段8によりH2とCOに分解し得るので、H2及びCOによりNOx吸蔵還元触媒5の表面上のNOxを効率良くN2に還元処理し、結果的に、様々な運転条件にかかわらず常に高いNOx低減率を得ることができる。 And Thus, according to the embodiment of the present invention, the fuel reforming since it can decompose into H 2 and CO by the catalyst structure 7 or plasma fuel reformer unit 8, the surface of the NOx storage reduction catalyst 5 by H 2 and CO The above NOx is efficiently reduced to N 2, and as a result, it is possible to always obtain a high NOx reduction rate regardless of various operating conditions.

又、燃料を、燃料改質触媒構造7又はプラズマ燃料改質手段8にてH2とCOに分解させ、反応性の高いH2及びCOにより比較的低い温度領域から高いNOx低減率を得ることができるので、例えば渋滞の多い都市内での徐行運転等のように低負荷で排気温度が低い運転状態が継続され易い運転条件下であっても、車外に排出される排気ガス中に含まれるNOxを従来より効果的に低減することができる。 Furthermore, the fuel at the fuel reforming catalyst structure 7 or plasma fuel reformer unit 8 is decomposed into H 2 and CO, obtain a high NOx reduction rate from a relatively low temperature region by highly reactive H 2 and CO Therefore, it is included in the exhaust gas that is discharged outside the vehicle even under operating conditions where low-exhaust and low-exhaust temperature driving conditions are likely to continue, such as slow driving in cities with heavy traffic. NOx can be reduced more effectively than before.

本発明の実施の形態は、排気流路における燃料改質触媒構造7又はプラズマ燃料改質手段8の上流側に、NOをNO2に酸化するプラズマ発生手段29を配置すると、プラズマ発生手段29により温度に関係なくNOをNO2に酸化し得るので、NOx吸蔵還元触媒5によるNOx吸蔵を容易にすることができる。 In the embodiment of the present invention, when the plasma generating means 29 for oxidizing NO into NO 2 is arranged upstream of the fuel reforming catalyst structure 7 or the plasma fuel reforming means 8 in the exhaust passage, the plasma generating means 29 Since NO can be oxidized to NO 2 regardless of the temperature, NOx occlusion by the NOx occlusion reduction catalyst 5 can be facilitated.

本発明の実施の形態において、プラズマ発生手段29は、制御装置33により、排気燃料比がリーン時にNOをNO2に酸化してNOx吸蔵還元触媒5によるNOx吸蔵を促進させるよう制御されると、NOx吸蔵還元触媒5によるNOx吸蔵を一層容易にすることができる。 In the embodiment of the present invention, when the plasma generation means 29 is controlled by the control device 33 to oxidize NO to NO 2 when the exhaust fuel ratio is lean and promote NOx occlusion by the NOx occlusion reduction catalyst 5, The NOx occlusion by the NOx occlusion reduction catalyst 5 can be further facilitated.

本発明の実施の形態において、燃料改質触媒構造7又はプラズマ燃料改質手段8は、制御装置33により、空燃比が燃料リッチ時に燃料をH2とCOに分解してNOx吸蔵還元触媒5のNOxを還元するよう制御されると、H2及びCOによりNOx吸蔵還元触媒5の表面上のNOxを一層効率良くN2に還元処理することができる。 In the embodiment of the present invention, the fuel reforming catalyst structure 7 or the plasma fuel reforming means 8 causes the control device 33 to decompose the fuel into H 2 and CO when the air-fuel ratio is rich in the fuel and to reduce the NOx storage reduction catalyst 5. When controlled to reduce NOx, it is possible to reduction treatment of NOx on more efficiently N 2 surface of the NOx storage reduction catalyst 5 by H 2 and CO.

本発明の実施の形態において、燃料改質触媒構造7又はプラズマ燃料改質手段8は、制御装置33により、排気温度が充分高い場合(350℃以上)には燃料を非分解で供給して瞬間的に燃料を濃くするよう制御されると、NOx吸蔵還元触媒5の表面上のNOxを適切にN2に還元処理することができる。 In the embodiment of the present invention, the fuel reforming catalyst structure 7 or the plasma fuel reforming means 8 supplies the fuel non-decomposingly when the exhaust temperature is sufficiently high (350 ° C. or higher) by the control device 33. manner when it is controlled to rich fuel, can be properly reduction to N 2 to NOx on the surface of the NOx storage reduction catalyst 5.

尚、本発明の排気浄化装置は、上述の形態例にのみ限定されるものではなく、本発明の要旨を逸脱しない範囲内において種々変更を加え得ることは勿論である。   Note that the exhaust emission control device of the present invention is not limited to the above-described embodiment, and it is needless to say that various modifications can be made without departing from the gist of the present invention.

本発明を実施する形態例であって燃料改質触媒構造を用いた場合を示す概略図である。It is the schematic which shows the case where it is an example of embodiment which implements this invention, and a fuel reforming catalyst structure is used. 本発明を実施する形態例であってプラズマ燃料改質手段を用いた場合を示す概略図である。It is the schematic which shows the case where it is an embodiment which implements this invention, and a plasma fuel reforming means is used. 本発明の燃料改質触媒構造を示す概略図である。It is the schematic which shows the fuel reforming catalyst structure of this invention. 本発明のプラズマ燃料改質手段を示す概略図である。It is the schematic which shows the plasma fuel reforming means of this invention.

符号の説明Explanation of symbols

2 排気マニホールド(排気流路)
4 排気管(排気流路)
5 NOx吸蔵還元触媒
7 燃料改質触媒構造
8 プラズマ燃料改質手段
29 プラズマ発生手段
2 Exhaust manifold (exhaust flow path)
4 Exhaust pipe (exhaust flow path)
5 NOx occlusion reduction catalyst 7 Fuel reforming catalyst structure 8 Plasma fuel reforming means 29 Plasma generating means

Claims (5)

排気流路の途中にNOx吸蔵還元触媒を装備してNOxを還元浄化するように構成した排気浄化装置であって、前記排気流路におけるNOx吸蔵還元触媒の上流側に、燃料をH2とCOに分解する燃料改質触媒構造又はプラズマ燃料改質手段を設けたことを特徴とする排気浄化装置。 In the middle of the exhaust passage equipped with a NOx storage reduction catalyst an exhaust purification apparatus that is configured to reduce and purify NOx, the upstream side of the NOx storage reduction catalyst in the exhaust passage, the fuel H 2 and CO An exhaust gas purification apparatus provided with a fuel reforming catalyst structure or plasma fuel reforming means that decomposes into a gas. 排気流路における燃料改質触媒構造又はプラズマ燃料改質手段の上流側に、NOをNO2に酸化するプラズマ発生手段を配置した請求項1に記載の排気浄化装置。 The exhaust emission control device according to claim 1, wherein a plasma generating means for oxidizing NO into NO 2 is disposed upstream of the fuel reforming catalyst structure or the plasma fuel reforming means in the exhaust passage. プラズマ発生手段は、排気燃料比がリーン時にNOをNO2に酸化してNOx吸蔵還元触媒によるNOx吸蔵を促進させるよう制御された請求項2に記載の排気浄化装置。 The exhaust emission control device according to claim 2, wherein the plasma generating means is controlled to oxidize NO to NO 2 when the exhaust fuel ratio is lean to promote NOx occlusion by the NOx occlusion reduction catalyst. 燃料改質触媒構造又はプラズマ燃料改質手段は、空燃比が燃料リッチ時に燃料をH2とCOに分解してNOx吸蔵還元触媒のNOxを還元するよう制御された請求項1に記載の排気浄化装置。 2. The exhaust gas purification according to claim 1, wherein the fuel reforming catalyst structure or the plasma fuel reforming means is controlled to reduce the NOx of the NOx occlusion reduction catalyst by decomposing the fuel into H 2 and CO when the air-fuel ratio is rich. apparatus. 燃料改質触媒構造又はプラズマ燃料改質手段は、排気温度が充分高い場合には燃料を非分解で供給して瞬間的に燃料を濃くするよう制御された請求項1に記載の排気浄化装置。   2. The exhaust emission control device according to claim 1, wherein the fuel reforming catalyst structure or the plasma fuel reforming means is controlled so that the fuel is supplied in an undecomposed manner and the fuel is instantly concentrated when the exhaust temperature is sufficiently high.
JP2004357732A 2004-12-08 2004-12-10 Exhaust purification device Pending JP2006161768A (en)

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JP2004357732A JP2006161768A (en) 2004-12-10 2004-12-10 Exhaust purification device
US11/721,057 US7913486B2 (en) 2004-12-08 2005-12-07 Exhaust emission control device
PCT/JP2005/022448 WO2006062124A1 (en) 2004-12-08 2005-12-07 Exhaust gas purification device
DE602005015897T DE602005015897D1 (en) 2004-12-08 2005-12-07 EXHAUST EMISSION DEVICE
EP05814697A EP1835137B1 (en) 2004-12-08 2005-12-07 Exhaust emission device

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