JP2005232975A - Exhaust emission control device - Google Patents

Exhaust emission control device Download PDF

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JP2005232975A
JP2005232975A JP2004039493A JP2004039493A JP2005232975A JP 2005232975 A JP2005232975 A JP 2005232975A JP 2004039493 A JP2004039493 A JP 2004039493A JP 2004039493 A JP2004039493 A JP 2004039493A JP 2005232975 A JP2005232975 A JP 2005232975A
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reduction catalyst
nox
storage reduction
nox storage
temperature
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Mitsuru Hosoya
満 細谷
Noboru Uchida
登 内田
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Hino Motors Ltd
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Hino Motors Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an exhaust emission control device capable of obtaining a high NOx reduction ratio notwithstanding the operating conditions. <P>SOLUTION: The exhaust emission control device is provided with an NOx occlusion reduction catalyst 5 midway along an exhaust pipe 4, and formed to reduce and purify NOx by adding a reducing agent (light oil 13) upstream of the NOx occlusion reduction catalyst 5. A burner means (an injection nozzle 17, a spark plug 26, a burner chamber 7) to ignite and burn by injecting an appropriate amount of fuel (light oil) into the upstream side of the NOx occlusion reduction catalyst 5 is installed upstream of the NOx occlusion reduction chamber 5. <P>COPYRIGHT: (C)2005,JPO&NCIPI

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、排気空燃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 carried out with an exhaust purification catalyst installed in the middle of the exhaust pipe. As this type of exhaust purification catalyst, NOx in exhaust gas is oxidized when the exhaust air-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、イリジウム・白金・バリウム・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, iridium / platinum / barium / alumina catalyst and the like are already known as having the above-mentioned properties.

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(機関をリッチ空燃比で運転)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機関をリッチ空燃比で運転することが困難である。 For example, when used in a gasoline engine, the operating air-fuel ratio of the engine is reduced (the engine is operated at a rich air-fuel ratio), thereby reducing the O 2 concentration in the exhaust gas and unburned HC in the exhaust gas. It is possible to promote the decomposition and release of NOx by increasing reducing components such as CO and CO. However, when the NOx storage reduction catalyst is used as an exhaust purification device of a diesel engine, it is difficult to operate the engine at a rich air-fuel ratio. is there.

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低減率を確保し得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 purification device that can always ensure a high NOx reduction rate regardless of operating conditions.

本発明は、排気管の途中にNOx吸蔵還元触媒を装備し且つ該NOx吸蔵還元触媒の上流側に還元剤を添加して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、NOx吸蔵還元触媒の上流側に適量の燃料を噴射して着火燃焼せしめるバーナ手段を設けたことを特徴とするものである。   The present invention relates to an exhaust purification device that is equipped with a NOx occlusion reduction catalyst in the middle of an exhaust pipe and is configured to reduce and purify NOx by adding a reducing agent upstream of the NOx occlusion reduction catalyst. A burner means for injecting an appropriate amount of fuel and igniting and burning it is provided upstream of the reduction catalyst.

而して、このようにすれば、NOx吸蔵還元触媒の表面上で還元剤が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であっても、バーナ手段によりNOx吸蔵還元触媒の上流側に適量の燃料を噴射して着火燃焼させれば、この燃焼により高温化された排気ガスがNOx吸蔵還元触媒に導入され、その触媒床温度が反応に必要な温度まで強制的に昇温される結果、現状の運転条件にかかわらずNOx吸蔵還元触媒の表面上で還元剤がO2と反応(燃焼)するのに必要な燃焼温度が確実に得られる。 Thus, in this way, the operating conditions are such that the combustion temperature (about 220 to 250 ° C.) necessary for the reducing agent to react (combust) with O 2 on the surface of the NOx storage reduction catalyst cannot be obtained. However, if an appropriate amount of fuel is injected upstream of the NOx storage reduction catalyst by the burner means and ignited and combusted, the exhaust gas heated to this temperature is introduced into the NOx storage reduction catalyst, and the catalyst bed temperature is As a result of forcibly raising the temperature to the temperature required for the reaction, the combustion temperature necessary for the reducing agent to react (combust) with O 2 on the surface of the NOx storage reduction catalyst is ensured regardless of the current operating conditions. can get.

また、本発明のバーナ手段は、NOx吸蔵還元触媒の上流側に適量の燃料を噴射する燃料噴射ノズルと、該燃料噴射ノズルの噴射口近傍に設けられた点火装置と、これら燃料噴射ノズル及び点火装置を所要の燃焼空間を確保して被包するバーナ室とにより構成することが可能である。   The burner means of the present invention includes a fuel injection nozzle for injecting an appropriate amount of fuel upstream of the NOx storage reduction catalyst, an ignition device provided in the vicinity of the injection port of the fuel injection nozzle, the fuel injection nozzle and the ignition It is possible to configure the apparatus with a burner chamber that encloses the required combustion space.

更に、本発明をより具体的に実施するにあたっては、例えば、NOx吸蔵還元触媒の触媒床温度を検出する温度センサと、該温度センサからの検出信号に基づき前記NOx吸蔵還元触媒の触媒床温度が所定温度以下である条件下で当該温度を超えるまでバーナ手段を着火燃焼させる制御装置とを備えることが好ましい。   Further, in carrying out the present invention more specifically, for example, a temperature sensor for detecting the catalyst bed temperature of the NOx storage reduction catalyst, and the catalyst bed temperature of the NOx storage reduction catalyst based on a detection signal from the temperature sensor, It is preferable to include a control device that ignites and burns the burner means until the temperature is exceeded under a condition that is equal to or lower than a predetermined temperature.

上記した本発明の排気浄化装置によれば、バーナ手段により適宜にNOx吸蔵還元触媒を加熱して該NOx吸蔵還元触媒の表面上で還元剤がO2と反応(燃焼)するのに必要な燃焼温度を確実に得ることができるので、運転条件にかかわらず常に高いNOx低減率を確保することができ、NOx吸蔵還元触媒を用いた排気浄化装置の実用性を大幅に向上することができるという優れた効果を奏し得る。 According to the exhaust gas purification apparatus of the present invention described above, the combustion necessary for the NOx storage reduction catalyst to be appropriately heated by the burner means and the reducing agent to react (combust) with O 2 on the surface of the NOx storage reduction catalyst. Since the temperature can be reliably obtained, a high NOx reduction rate can always be ensured regardless of the operating conditions, and the practicality of the exhaust purification apparatus using the NOx storage reduction catalyst can be greatly improved. The effects 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及び図2は本発明を実施する形態の一例を示すもので、図1に示す如く、本形態例の排気浄化装置においては、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がケーシング6に抱持されて装備されており、該ケーシング6の前段には、後で詳述するバーナ室7が形成されている。   FIG. 1 and FIG. 2 show an example of an embodiment for carrying out the present invention. As shown in FIG. 1, in the exhaust purification apparatus of this embodiment, the exhaust gas discharged from the diesel engine 1 through the exhaust manifold 2 is shown. A NOx occlusion reduction catalyst 5 having a flow-through type honeycomb structure is provided in the middle of the exhaust pipe 4 through which the gas flow 3 circulates and is mounted on the casing 6. A burner chamber 7 is formed.

更に、前記バーナ室7より上流側の排気管4に還元剤噴射ノズル8が貫通設置されていると共に、該還元剤噴射ノズル8と所要場所に設けた軽油タンク9との間が軽油供給管10により接続されており、該軽油供給管10の途中に装備した供給ポンプ11の駆動と軽油噴射弁12の開作動とにより軽油タンク9内の軽油13を還元剤として還元剤噴射ノズル8を介しケーシング6の入側に添加し得るようにしてある。   Further, a reducing agent injection nozzle 8 is provided through the exhaust pipe 4 upstream of the burner chamber 7, and a light oil supply pipe 10 is provided between the reducing agent injection nozzle 8 and a light oil tank 9 provided at a required location. And the casing of the light oil tank 9 through the reducing agent injection nozzle 8 using the light oil 13 in the light oil tank 9 as a reducing agent by driving the supply pump 11 provided in the middle of the light oil supply pipe 10 and opening the light oil injection valve 12. 6 can be added to the inlet side.

また、前記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14が装備されており、該回転センサ14からの回転数信号14aと、アクセルセンサ15(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15aとが制御装置16に入力されるようになっている。   Further, the diesel engine 1 is equipped with a rotation sensor 14 for detecting the engine rotation speed, and a rotation speed signal 14a from the rotation sensor 14 and an accelerator sensor 15 (a sensor for detecting the depression angle of the accelerator pedal). ) Is input to the control device 16.

一方、制御装置16においては、前述した回転センサ14からの回転数信号14aと、アクセルセンサ15からの負荷信号15aとから判断される現在の運転状態に基づきNOxの発生量が推定されると共に、その推定されたNOxの発生量に見合う軽油13の添加量が更に算出され、必要量の軽油13の添加が実行されるように前記制御装置16から供給ポンプ11への駆動指令信号11aと軽油噴射弁12への開弁指令信号12aとが出力されるようになっている。   On the other hand, in the control device 16, the amount of NOx generated is estimated based on the current operating state determined from the rotation speed signal 14a from the rotation sensor 14 and the load signal 15a from the accelerator sensor 15, and The addition amount of the light oil 13 corresponding to the estimated NOx generation amount is further calculated, and the drive command signal 11a and the light oil injection from the control device 16 to the supply pump 11 are executed so that the required amount of the light oil 13 is added. A valve opening command signal 12a to the valve 12 is output.

更に、前記バーナ室7の内部には、NOx吸蔵還元触媒5の上流側に適量の軽油13を噴射する燃料噴射ノズル17が貫通設置されていると共に、該燃料噴射ノズル17と前記供給ポンプ11との間が枝管18により接続されており、該枝管18の途中に装備した軽油調量弁19の開作動と前記供給ポンプ11の駆動とにより軽油タンク9内の軽油13をバーナ用燃料として燃料噴射ノズル17から噴射し得るようにしてある。   Further, a fuel injection nozzle 17 for injecting an appropriate amount of light oil 13 is provided through the burner chamber 7 upstream of the NOx storage reduction catalyst 5, and the fuel injection nozzle 17, the supply pump 11, Are connected by a branch pipe 18, and the light oil 13 in the light oil tank 9 is used as fuel for the burner by opening the light oil metering valve 19 provided in the middle of the branch pipe 18 and driving the supply pump 11. The fuel can be injected from the fuel injection nozzle 17.

また、この燃料噴射ノズル17の噴射口近傍には、イグニッションコイル20から出力される高電圧信号26aにより放電を起こすスパークプラグ26が、噴射口から噴射された軽油13に点火するための点火装置として配設されており、このスパークプラグ26と、前記燃料噴射ノズル17と、これらを所要の燃焼空間を確保して被包するバーナ室7とによりバーナ手段が構成されるようになっている。   Further, in the vicinity of the injection port of the fuel injection nozzle 17, a spark plug 26 that generates a discharge by a high voltage signal 26a output from the ignition coil 20 serves as an ignition device for igniting the light oil 13 injected from the injection port. The spark plug 26, the fuel injection nozzle 17, and the burner chamber 7 that encloses the spark plug 26 while securing a required combustion space are configured.

一方、前記NOx吸蔵還元触媒5のケーシング6には、NOx吸蔵還元触媒5の入口排気温度を検出する温度センサ21と、NOx吸蔵還元触媒5の出口排気温度を検出する温度センサ22とが装備されており、これら各温度センサ21,22からの検出信号21a,22aが前記制御装置16に入力されるようになっている。   On the other hand, the casing 6 of the NOx storage reduction catalyst 5 is equipped with a temperature sensor 21 for detecting the inlet exhaust temperature of the NOx storage reduction catalyst 5 and a temperature sensor 22 for detecting the outlet exhaust temperature of the NOx storage reduction catalyst 5. The detection signals 21 a and 22 a from these temperature sensors 21 and 22 are input to the control device 16.

そして、制御装置16においては、前述した各温度センサ21,22からの検出信号21a,22aに基づきNOx吸蔵還元触媒5の入口排気温度と出口排気温度との温度差が求められ、更には、この温度差に基づきNOx吸蔵還元触媒5の触媒床温度が推定(間接的に検出)されると共に、その推定された触媒床温度が所定温度以下である条件下で当該温度を超えるまでバーナ燃焼を実行させるべく軽油調量弁19への開弁指令信号19aとイグニッションコイル20への通電指令信号20aが出力されるようになっている。   The control device 16 obtains the temperature difference between the inlet exhaust temperature and the outlet exhaust temperature of the NOx storage reduction catalyst 5 based on the detection signals 21a and 22a from the temperature sensors 21 and 22 described above. Based on the temperature difference, the catalyst bed temperature of the NOx occlusion reduction catalyst 5 is estimated (indirectly detected), and burner combustion is performed until the estimated catalyst bed temperature exceeds the predetermined temperature under the condition that the estimated catalyst bed temperature is below a predetermined temperature. In order to achieve this, a valve opening command signal 19a to the light oil metering valve 19 and an energization command signal 20a to the ignition coil 20 are output.

ただし、ここに図示している例では、NOx吸蔵還元触媒5の内部に温度センサの検温部を差し込んで触媒床温度を直接検温することが技術的に難しいことから、NOx吸蔵還元触媒5の前後に温度センサ21,22を配置して間接的に触媒床温度を検出(推定)する形式を採用しているが、可能であればNOx吸蔵還元触媒5の内部に温度センサの検温部を差し込んで触媒床温度を直接検温するようにしても良い。   However, in the example shown here, it is technically difficult to directly detect the temperature of the catalyst bed by inserting the temperature sensor of the temperature sensor inside the NOx storage reduction catalyst 5. However, the temperature sensor 21 and 22 are arranged to indirectly detect (estimate) the catalyst bed temperature. If possible, a temperature sensor of the temperature sensor is inserted into the NOx storage reduction catalyst 5. The catalyst bed temperature may be directly measured.

尚、図1中における23はターボチャージャ、24は吸気管、25はインタークーラを示す。   In FIG. 1, reference numeral 23 denotes a turbocharger, 24 denotes an intake pipe, and 25 denotes an intercooler.

而して、このように排気浄化装置を構成すれば、NOx吸蔵還元触媒5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であっても、各温度センサ21,22からの検出信号21a,22aに基づいて、制御装置16から軽油調量弁19への開弁指令信号19aとイグニッションコイル20への通電指令信号20aが出力され、バーナ手段を成す燃料噴射ノズル17からNOx吸蔵還元触媒5の上流側に適量の軽油13が噴射されてスパークプラグ26により着火燃焼されるので、この燃焼によりバーナ室7内で高温化された排気ガス3がNOx吸蔵還元触媒5に導入され、その触媒床温度が反応に必要な温度まで強制的に昇温されることになる。 Thus, if the exhaust gas purification apparatus is configured in this way, a combustion temperature (about 220 to 250 ° C.) necessary for HC to react (combust) with O 2 on the surface of the NOx storage reduction catalyst 5 can be obtained. Even under non-operating conditions, based on the detection signals 21a and 22a from the temperature sensors 21 and 22, the valve opening command signal 19a from the control device 16 to the light oil metering valve 19 and the energization command signal to the ignition coil 20 are provided. 20a is output and an appropriate amount of light oil 13 is injected from the fuel injection nozzle 17 constituting the burner means to the upstream side of the NOx storage reduction catalyst 5 and ignited and combusted by the spark plug 26. The converted exhaust gas 3 is introduced into the NOx occlusion reduction catalyst 5, and the temperature of the catalyst bed is forcibly raised to the temperature required for the reaction.

この結果、現状の運転条件にかかわらずNOx吸蔵還元触媒5の表面上でHCがO2と反応(燃焼)するのに必要な燃焼温度が確実に得られるので、制御装置16からの駆動指令信号11aにより供給ポンプ11を駆動させると共に、開弁指令信号12aにより軽油噴射弁12を開作動させて、現在の運転状態から推定したNOxの発生量に見合う添加量の軽油13を還元剤噴射ノズル8から噴射させると、還元剤として添加した軽油13から生成されたHCがNOx吸蔵還元触媒5の表面上で排気ガス3中のO2と反応(燃焼)し、これによりNOx吸蔵還元触媒5の周囲の雰囲気中におけるO2濃度がほぼ零となってNOxの分解放出が開始され、そのままNOx吸蔵還元触媒5の表面上で残余のHCによりNOxが効率良くN2に還元処理されることになる。 As a result, it is possible to reliably obtain the combustion temperature necessary for HC to react (combust) with O 2 on the surface of the NOx storage reduction catalyst 5 regardless of the current operating conditions. The supply pump 11 is driven by 11a, and the light oil injection valve 12 is opened by the valve opening command signal 12a, so that the addition amount of light oil 13 corresponding to the amount of NOx estimated from the current operation state is reduced. HC generated from the light oil 13 added as a reducing agent reacts (combusts) with O 2 in the exhaust gas 3 on the surface of the NOx storage reduction catalyst 5, and thereby the surroundings of the NOx storage reduction catalyst 5. this O 2 concentration in the atmosphere is started substantially zero and becomes an exploded release of NOx, the NOx by residual HC is reduced processed efficiently N 2 as it on the surface of the NOx storage reduction catalyst 5 To become.

従って、以上に述べた如き形態例によれば、燃料噴射ノズル17とスパークプラグ26とバーナ室7とから成るバーナ手段により適宜にNOx吸蔵還元触媒5を加熱して、該NOx吸蔵還元触媒5の表面上でHCがO2と反応(燃焼)するのに必要な燃焼温度を確実に得ることができるので、運転条件にかかわらず常に高いNOx低減率を確保することができ、NOx吸蔵還元触媒5を用いた排気浄化装置の実用性を大幅に向上することができる。 Therefore, according to the embodiment as described above, the NOx storage reduction catalyst 5 is appropriately heated by the burner means including the fuel injection nozzle 17, the spark plug 26, and the burner chamber 7, so that the NOx storage reduction catalyst 5 Since the combustion temperature necessary for HC to react (combust) with O 2 on the surface can be reliably obtained, a high NOx reduction rate can always be ensured regardless of the operating conditions, and the NOx storage reduction catalyst 5 The practicality of the exhaust gas purification apparatus using can be greatly improved.

事実、本発明者等が行った実験結果によれば、図2のグラフに示す如く、先に説明した本形態例の装置構成でバーナ手段による加熱支援を実施したケースXと、バーナ手段を装備せずにNOx吸蔵還元触媒5だけを装備したケースYとを比較したところ、ケースYよりもケースXの方が低負荷領域(排気温度の低い運転領域)から高いNOx低減率を得られることが実証されている。   In fact, according to the results of experiments conducted by the present inventors, as shown in the graph of FIG. 2, the case X in which the heating support by the burner means is implemented in the apparatus configuration of the present embodiment described above and the burner means are provided. In comparison with the case Y equipped only with the NOx occlusion reduction catalyst 5, the case X can obtain a higher NOx reduction rate than the case Y from the low load region (the operation region where the exhaust temperature is low). Proven.

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、還元剤として添加される燃料には、一般的なディーゼルエンジン用燃料である軽油を用いる以外に、灯油等の異種燃料を用いても良いこと、その他、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。   The exhaust emission control device of the present invention is not limited to the above-described embodiment. For fuel added as a reducing agent, in addition to using light oil that is a general diesel engine fuel, kerosene or the like. Of course, different types of fuels may be used, and various modifications can be made without departing from the scope of the present invention.

本発明を実施する形態の一例を示す概略図である。It is the schematic which shows an example of the form which implements this invention. NOx低減率と負荷との関係を比較例と共に示すグラフである。It is a graph which shows the relationship between a NOx reduction rate and load with a comparative example.

符号の説明Explanation of symbols

3 排気ガス
4 排気管
5 NOx吸蔵還元触媒
7 バーナ室(バーナ手段)
8 還元剤噴射ノズル
13 軽油(還元剤:バーナ用燃料)
16 制御装置
17 燃料噴射ノズル(バーナ手段)
21 温度センサ
21a 検出信号
22 温度センサ
22a 検出信号
26 スパークプラグ(点火装置:バーナ手段)
3 Exhaust gas 4 Exhaust pipe 5 NOx storage reduction catalyst 7 Burner chamber (burner means)
8 Reducing agent injection nozzle 13 Light oil (Reducing agent: Fuel for burner)
16 Control device 17 Fuel injection nozzle (burner means)
21 temperature sensor 21a detection signal 22 temperature sensor 22a detection signal 26 spark plug (ignition device: burner means)

Claims (3)

排気管の途中にNOx吸蔵還元触媒を装備し且つ該NOx吸蔵還元触媒の上流側に還元剤を添加して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、NOx吸蔵還元触媒の上流側に適量の燃料を噴射して着火燃焼せしめるバーナ手段を設けたことを特徴とする排気浄化装置。   An exhaust gas purification apparatus equipped with a NOx storage reduction catalyst in the middle of an exhaust pipe and configured to reduce and purify NOx by adding a reducing agent upstream of the NOx storage reduction catalyst, upstream of the NOx storage reduction catalyst An exhaust emission control device comprising burner means for injecting and burning an appropriate amount of fuel on the side. NOx吸蔵還元触媒の上流側に適量の燃料を噴射する燃料噴射ノズルと、該燃料噴射ノズルの噴射口近傍に設けられた点火装置と、これら燃料噴射ノズル及び点火装置を所要の燃焼空間を確保して被包するバーナ室とによりバーナ手段を構成したことを特徴とする請求項1に記載の排気浄化装置。   A fuel injection nozzle that injects an appropriate amount of fuel upstream of the NOx storage reduction catalyst, an ignition device provided in the vicinity of the injection port of the fuel injection nozzle, and the fuel injection nozzle and the ignition device to ensure a required combustion space. 2. The exhaust emission control device according to claim 1, wherein a burner means is constituted by the burner chamber to be encapsulated. NOx吸蔵還元触媒の触媒床温度を検出する温度センサと、該温度センサからの検出信号に基づき前記NOx吸蔵還元触媒の触媒床温度が所定温度以下である条件下で当該温度を超えるまでバーナ手段を着火燃焼させる制御装置とを備えたことを特徴とする請求項1又は2に記載の排気浄化装置。   A temperature sensor for detecting the catalyst bed temperature of the NOx storage reduction catalyst, and a burner means based on a detection signal from the temperature sensor until the catalyst bed temperature of the NOx storage reduction catalyst is lower than a predetermined temperature until the temperature exceeds the temperature. The exhaust emission control device according to claim 1, further comprising a control device that performs ignition and combustion.
JP2004039493A 2004-02-17 2004-02-17 Exhaust emission control device Pending JP2005232975A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009197713A (en) * 2008-02-22 2009-09-03 Yanmar Co Ltd Exhaust gas purifier
WO2011125207A1 (en) 2010-04-08 2011-10-13 トヨタ自動車株式会社 Exhaust gas purification system for internal combustion engine
WO2012009496A2 (en) * 2010-07-15 2012-01-19 Faurecia Emissions Control Technologies Fuel fired burner for vehicle exhaust component
US20130041571A1 (en) * 2010-03-11 2013-02-14 Toyota Jidosha Kabushiki Kaisha Control device for internal combustion engine

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009197713A (en) * 2008-02-22 2009-09-03 Yanmar Co Ltd Exhaust gas purifier
US20130041571A1 (en) * 2010-03-11 2013-02-14 Toyota Jidosha Kabushiki Kaisha Control device for internal combustion engine
WO2011125207A1 (en) 2010-04-08 2011-10-13 トヨタ自動車株式会社 Exhaust gas purification system for internal combustion engine
US9206724B2 (en) 2010-04-08 2015-12-08 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification system for internal combustion engine
WO2012009496A2 (en) * 2010-07-15 2012-01-19 Faurecia Emissions Control Technologies Fuel fired burner for vehicle exhaust component
WO2012009496A3 (en) * 2010-07-15 2012-04-19 Faurecia Emissions Control Technologies Fuel fired burner for vehicle exhaust component
CN102985646A (en) * 2010-07-15 2013-03-20 佛吉亚排放控制技术美国有限公司 Fuel fired burner for vehicle exhaust component
US9506385B2 (en) 2010-07-15 2016-11-29 Faurecia Emissions Control Technologies, Usa, Llc Fuel fired burner for vehicle exhaust component

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