JP2016176428A - Exhaust emission control device for engine - Google Patents

Exhaust emission control device for engine Download PDF

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JP2016176428A
JP2016176428A JP2015058253A JP2015058253A JP2016176428A JP 2016176428 A JP2016176428 A JP 2016176428A JP 2015058253 A JP2015058253 A JP 2015058253A JP 2015058253 A JP2015058253 A JP 2015058253A JP 2016176428 A JP2016176428 A JP 2016176428A
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reduction catalyst
engine
nox
selective reduction
nitrogen oxide
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JP6663126B2 (en
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洋 阿野田
Hiroshi Anoda
洋 阿野田
田代 圭介
Keisuke Tashiro
圭介 田代
川島 一仁
Kazuhito Kawashima
川島  一仁
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Mitsubishi Motors Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

PROBLEM TO BE SOLVED: To improve exhaust emission control performance.SOLUTION: An exhaust passage 10 of an engine 2 includes: an NOx occlusion catalyst 11; and a selective reduction catalyst 13 provided downstream of the NOx occlusion catalyst 11 for reducing and eliminating NOx by using ammonia generated from urea water. An engine control unit 30 of the engine performs purge control for reducing and eliminating NOx occluded in the NOx occlusion catalyst 11 by increasing an exhaust temperature of the engine 2 and making an air-fuel ratio of exhaust gas stoichiometric or rich when NOx occlusion amount Qa of the NOx occlusion catalyst 11 exceeds a predetermined value A, and performs temperature increase control for supplying ammonia to the selective reduction catalyst 13 by making the air-fuel ratio of the exhaust gas lean and increasing the exhaust temperature to an activation temperature of the selective reduction catalyst 13 or higher when the NOx occlusion amount Qa becomes larger than a predetermined value B larger than the predetermined value A.SELECTED DRAWING: Figure 1

Description

本発明は、排気中の窒素酸化物を浄化する排気浄化触媒を備えたエンジンの排気浄化装置に関する。   The present invention relates to an exhaust emission control device for an engine provided with an exhaust purification catalyst that purifies nitrogen oxides in exhaust gas.

エンジンの排気通路には、排気を浄化するための排気浄化装置が備えられている。例えば、エンジンの排気中のNOx(窒素酸化物)を浄化するために、NOx吸蔵触媒や選択還元触媒等の排気浄化触媒が開発されている。
NOx吸蔵触媒は、リーン雰囲気下でNOxを吸蔵し、リッチ雰囲気下でNOxを窒素に還元する。なお、NOx吸蔵触媒は、低温領域で吸蔵量を多く確保でき、高温領域で吸蔵量が低下する性質を有している。一方、選択還元触媒は、主に高温領域でアンモニア等の還元剤を使用して排気中のNOxを窒素に還元する。
The exhaust passage of the engine is provided with an exhaust purification device for purifying the exhaust. For example, exhaust purification catalysts such as NOx storage catalysts and selective reduction catalysts have been developed to purify NOx (nitrogen oxides) in engine exhaust.
The NOx storage catalyst stores NOx under a lean atmosphere and reduces NOx to nitrogen under a rich atmosphere. Note that the NOx storage catalyst has a property that a large storage amount can be secured in a low temperature region and the storage amount decreases in a high temperature region. On the other hand, the selective reduction catalyst reduces NOx in the exhaust to nitrogen mainly using a reducing agent such as ammonia in a high temperature region.

例えば特許文献1には、ディーゼルエンジンの排気通路に、排気中のPM(粒子状物質)を捕集するディーゼルパティキュレートフィルタを設け、ディーゼルパティキュレートフィルタの上流側の排気通路にNOx吸蔵触媒を備えるとともに、ディーゼルパティキュレートフィルタの下流側の排気通路に選択還元触媒を備えた排気浄化装置が開示されている。   For example, in Patent Document 1, a diesel particulate filter that collects PM (particulate matter) in exhaust gas is provided in an exhaust passage of a diesel engine, and a NOx storage catalyst is provided in an exhaust passage upstream of the diesel particulate filter. At the same time, an exhaust emission control device including a selective reduction catalyst in an exhaust passage downstream of a diesel particulate filter is disclosed.

特許第4730336号公報Japanese Patent No. 4730336

ところで、排気通路にNOx吸蔵触媒を備えたエンジンでは、NOx吸蔵触媒に吸蔵したNOxを除去するために、例えばエンジンの燃料噴射制御によってNOx吸蔵触媒にリッチ空燃比の排気を供給するNOxパージが必要に応じて行われる。
しかしながら、例えば低負荷運転が続いてNOx吸蔵触媒の温度が低下している場合には、NOxパージをすることができず、NOx吸蔵触媒におけるNOx吸蔵量が更に増加する。このようにNOx吸蔵量が増加すると、その後例えば高負荷運転等により排気温度が上昇してNOxパージが開始されたときに、NOx吸蔵触媒からNOxが流出してしまう。特許文献1のようにNOx吸蔵触媒の下流に選択還元触媒を設けている構成では、NOx吸蔵触媒から流出したNOxを選択還元触媒にて還元除去可能であるものの、低負荷運転が続いていた状態では選択還元触媒の温度が低下しており、選択還元触媒においてNOxを十分に除去できず下流に流出してしまうといった虞がある。
By the way, in an engine provided with a NOx storage catalyst in the exhaust passage, in order to remove NOx stored in the NOx storage catalyst, for example, NOx purge for supplying exhaust gas of rich air-fuel ratio to the NOx storage catalyst by engine fuel injection control is required. Is done according to.
However, for example, when the temperature of the NOx storage catalyst is lowered due to low load operation, NOx purge cannot be performed, and the NOx storage amount in the NOx storage catalyst further increases. If the NOx occlusion amount increases in this way, NOx will flow out from the NOx occlusion catalyst when the exhaust gas temperature then rises due to, for example, high load operation or the like and NOx purge is started. In the configuration in which the selective reduction catalyst is provided downstream of the NOx storage catalyst as in Patent Document 1, the NOx flowing out from the NOx storage catalyst can be reduced and removed by the selective reduction catalyst, but the low load operation has continued. Then, the temperature of the selective reduction catalyst is lowered, and there is a possibility that NOx cannot be sufficiently removed in the selective reduction catalyst and flows out downstream.

本発明はこのような問題点を解決するためになされたもので、排気通路に窒素酸化物吸蔵還元触媒及び選択還元触媒を備えたエンジンにおいて、排気浄化性能の優れた排気浄化装置を提供することにある。   The present invention has been made to solve such problems, and provides an exhaust purification device having excellent exhaust purification performance in an engine provided with a nitrogen oxide storage reduction catalyst and a selective reduction catalyst in an exhaust passage. It is in.

上記の目的を達成するために、請求項1のエンジンの排気浄化装置では、エンジンの排気通路に設けられ、排気中の窒素酸化物を吸蔵する窒素酸化物吸蔵還元触媒と、前記窒素酸化物吸蔵還元触媒の下流側の前記排気通路に設けられ、還元剤を用いて窒素酸化物を還元除去する選択還元触媒と、前記選択還元触媒に前記還元剤を供給する還元剤供給部と、前記窒素酸化物吸蔵還元触媒の窒素酸化物吸蔵量を推定する窒素酸化物吸蔵量推定部と、前記窒素酸化物吸蔵量が所定の第1の吸蔵量より多くなった状態で、所定のパージ条件が成立した場合には、排気の空燃比をストイキまたはリッチにして、前記窒素酸化物吸蔵還元触媒に吸蔵した前記窒素酸化物を還元するパージ制御を実行するパージ制御部と、前記窒素酸化物吸蔵量が前記第1の吸蔵量より大きくなった状態で、前記パージ条件が成立しない場合には、排気の空燃比をリーンにした状態で、前記還元剤供給部により前記還元剤を供給して前記選択還元触媒に前記還元剤を供給させるとともに前記選択還元触媒の温度を所定温度以上に上昇させる昇温制御を実行する昇温制御部と、を備えることを特徴とする。   In order to achieve the above object, in the exhaust emission control device for an engine according to claim 1, a nitrogen oxide storage and reduction catalyst provided in an exhaust passage of the engine for storing nitrogen oxide in the exhaust, and the nitrogen oxide storage A selective reduction catalyst provided in the exhaust passage on the downstream side of the reduction catalyst, for reducing and removing nitrogen oxides using a reducing agent; a reducing agent supply unit for supplying the reducing agent to the selective reduction catalyst; and the nitrogen oxidation A nitrogen oxide storage amount estimation unit for estimating the nitrogen oxide storage amount of the material storage reduction catalyst, and a predetermined purge condition is established in a state where the nitrogen oxide storage amount is greater than a predetermined first storage amount. In this case, a purge control unit that performs a purge control for reducing the nitrogen oxide stored in the nitrogen oxide storage reduction catalyst by making the air-fuel ratio of the exhaust stoichiometric or rich, and the nitrogen oxide storage amount is the First If the purge condition is not satisfied in a state where the amount is greater than the storage amount, the reducing agent is supplied by the reducing agent supply unit while the exhaust air-fuel ratio is lean, and the reduction catalyst is supplied to the selective reduction catalyst. And a temperature increase control unit that executes temperature increase control for supplying the agent and increasing the temperature of the selective reduction catalyst to a predetermined temperature or higher.

また、好ましくは、前記パージ制御部は、前記昇温制御を実行中に前記パージ条件が成立した際には、前記昇温制御から前記パージ制御に強制的に切換えるとよい。
また、好ましくは、前記昇温制御を、前記エンジンの吸気量の絞り及び前記エンジンの燃料噴射量の増加の少なくともいずれか一方により行うとよい。
また、好ましくは、前記還元剤供給部は、前記選択還元触媒の上流側の前記排気通路に尿素水溶液を供給して、当該尿素水溶液が加水分解して得られるアンモニアを前記選択還元触媒に供給するとよい。
Preferably, the purge control unit forcibly switches from the temperature increase control to the purge control when the purge condition is satisfied during the temperature increase control.
Preferably, the temperature increase control is performed by at least one of throttle of the intake air amount of the engine and increase of the fuel injection amount of the engine.
Preferably, the reducing agent supply unit supplies an aqueous urea solution to the exhaust passage upstream of the selective reduction catalyst, and supplies ammonia obtained by hydrolysis of the aqueous urea solution to the selective reduction catalyst. Good.

また、好ましくは、前記エンジンの負荷が所定値以上である場合には、前記窒素酸化物吸蔵量に拘わらず、前記昇温制御を実行するとよい。   Preferably, when the engine load is equal to or higher than a predetermined value, the temperature increase control is executed regardless of the nitrogen oxide storage amount.

本発明のエンジンの排気浄化装置によれば、排気通路に低温領域で浄化効率の高い窒素酸化物吸蔵還元触媒と高温領域で浄化効率の高い選択還元触媒が設けられているので、広範囲の温度領域で浄化効率を向上させることができる。更に、窒素酸化物の下流側に選択還元触媒が設けられているので、窒素酸化物吸蔵還元触媒から窒素酸化物が流出しても選択還元触媒によって還元除去することができる。   According to the exhaust purification device for an engine of the present invention, the exhaust passage is provided with the nitrogen oxide storage reduction catalyst having a high purification efficiency in the low temperature region and the selective reduction catalyst having a high purification efficiency in the high temperature region. Thus, the purification efficiency can be improved. Furthermore, since the selective reduction catalyst is provided on the downstream side of the nitrogen oxide, even if the nitrogen oxide flows out from the nitrogen oxide storage reduction catalyst, it can be reduced and removed by the selective reduction catalyst.

特に、窒素酸化物吸蔵還元触媒が低温で窒素酸化物の還元除去が不能であってパージ条件が成立せずに、窒素酸化物吸蔵量の吸蔵量が多くなった状態では、排気の空燃比をリーンにして排気温度を選択還元触媒の所定温度以上に上昇させる昇温制御を実行することで、燃料消費を抑えつつ選択還元触媒での浄化をすぐに可能にするよう準備させることができる。これにより、パージ制御が開始されたときに、窒素酸化物吸蔵還元触媒から窒素酸化物が流出したとしても、選択還元触媒にて十分に窒素酸化物を還元除去することができ、大気中への窒素酸化物の排出を減少させることができる。   In particular, in a state where the nitrogen oxide storage reduction catalyst cannot reduce and remove nitrogen oxides at low temperatures and the purge condition is not satisfied, and the storage amount of the nitrogen oxide storage amount increases, the air-fuel ratio of the exhaust gas is reduced. By executing the temperature raising control that leans and raises the exhaust temperature to a predetermined temperature or higher of the selective reduction catalyst, it is possible to prepare to immediately enable purification with the selective reduction catalyst while suppressing fuel consumption. Thereby, even when nitrogen oxide flows out of the nitrogen oxide storage reduction catalyst when the purge control is started, the selective reduction catalyst can sufficiently reduce and remove the nitrogen oxide, Nitrogen oxide emissions can be reduced.

本発明の実施形態におけるエンジンの吸排気系の概略構成図である。1 is a schematic configuration diagram of an intake / exhaust system of an engine in an embodiment of the present invention. 本実施形態のエンジンコントロールユニットにおける排気浄化装置の制御手順を示すフローチャートである。It is a flowchart which shows the control procedure of the exhaust gas purification apparatus in the engine control unit of this embodiment.

以下、図面に基づき本発明の実施形態について説明する。
図1は、本発明の排気浄化装置1が適用された第1の実施形態のディーゼルエンジン(以下、エンジン2という)の吸排気系の概略構成図である。
エンジン2は、走行駆動源として車両に搭載されており、多気筒の筒内直接噴射式エンジンであって、図1では簡略して1つの気筒のみ記載している。エンジン2は、各気筒に設けられた燃料噴射ノズル3から、任意の噴射時期及び噴射量で各気筒の燃焼室4内に燃料を噴射可能な構成となっている。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a schematic configuration diagram of an intake / exhaust system of a diesel engine (hereinafter referred to as an engine 2) according to a first embodiment to which an exhaust emission control device 1 of the present invention is applied.
The engine 2 is mounted on a vehicle as a travel drive source, and is a multi-cylinder direct injection type engine. In FIG. 1, only one cylinder is illustrated in a simplified manner. The engine 2 is configured to be able to inject fuel into the combustion chamber 4 of each cylinder at an arbitrary injection timing and injection amount from a fuel injection nozzle 3 provided in each cylinder.

エンジン2の吸気通路5には、新気の流量を調整するための電子制御スロットルバルブ6が設けられている。
エンジン2の排気通路10には、エンジン2から下流に向かって順番に、NOx吸蔵触媒11(窒素酸化物吸蔵還元触媒)、ディーゼルパティキュレートフィルタ12、選択還元触媒13が設けられている。
An electronic control throttle valve 6 for adjusting the flow rate of fresh air is provided in the intake passage 5 of the engine 2.
In the exhaust passage 10 of the engine 2, a NOx storage catalyst 11 (nitrogen oxide storage reduction catalyst), a diesel particulate filter 12, and a selective reduction catalyst 13 are provided in order from the engine 2 toward the downstream.

ディーゼルパティキュレートフィルタ12と選択還元触媒13との間の排気通路10には、尿素水(尿素水溶液)を噴射供給する尿素水インジェクタ14(還元剤供給部)が設けられている。尿素水インジェクタ14には、車両に搭載した図示しない尿素水タンクから尿素水が供給される。
尿素水インジェクタ14から排気通路10内に噴射された尿素水が排気の熱によって加水分解されてアンモニアを発生し選択還元触媒13に到達するように、尿素水インジェクタ14の噴射位置が設定されている。
The exhaust passage 10 between the diesel particulate filter 12 and the selective reduction catalyst 13 is provided with a urea water injector 14 (reducing agent supply unit) that injects and supplies urea water (urea aqueous solution). Urea water is supplied to the urea water injector 14 from a urea water tank (not shown) mounted on the vehicle.
The injection position of the urea water injector 14 is set so that the urea water injected from the urea water injector 14 into the exhaust passage 10 is hydrolyzed by the heat of the exhaust to generate ammonia and reach the selective reduction catalyst 13. .

NOx吸蔵触媒11は、排気中の窒素酸化物(以下、NOx)を貯留し、高温リッチ雰囲気下でNOxを還元除去する。
ディーゼルパティキュレートフィルタ12は、排気中の黒鉛を主成分とする微粒子状物資を捕集する。
選択還元触媒13は、尿素水から生成したアンモニアを還元剤として用いて排気中のNOxを還元浄化する。
The NOx storage catalyst 11 stores nitrogen oxide (hereinafter referred to as NOx) in the exhaust, and reduces and removes NOx under a high temperature rich atmosphere.
The diesel particulate filter 12 collects particulate matter whose main component is graphite in the exhaust gas.
The selective reduction catalyst 13 reduces and purifies NOx in the exhaust gas using ammonia generated from urea water as a reducing agent.

また、エンジン2には、EGR装置15が備えられている。EGR装置15は、吸気通路5と排気通路10とを連通するEGR通路16と、EGR通路16を開閉するEGRバルブ17とにより構成されている。
更に、エンジン2には、エンジン2の回転速度を検出する回転速度センサ20が設けられている。エンジン2の吸気通路5には、吸気流量を検出するエアフローセンサ21が設けられている。選択還元触媒13には、選択還元触媒13の温度を検出する選択還元触媒温度センサ22が設けられている。
The engine 2 is provided with an EGR device 15. The EGR device 15 includes an EGR passage 16 that connects the intake passage 5 and the exhaust passage 10, and an EGR valve 17 that opens and closes the EGR passage 16.
Further, the engine 2 is provided with a rotation speed sensor 20 that detects the rotation speed of the engine 2. An air flow sensor 21 that detects an intake air flow rate is provided in the intake passage 5 of the engine 2. The selective reduction catalyst 13 is provided with a selective reduction catalyst temperature sensor 22 that detects the temperature of the selective reduction catalyst 13.

エンジンコントロールユニット30(窒素酸化物吸蔵量推定部、パージ制御部、昇温制御部)は、入出力装置、記憶装置(ROM、RAM、不揮発性RAM等)、タイマ及び中央演算処理装置(CPU)等を含んで構成され、回転速度センサ20、エアフローセンサ21、選択還元触媒温度センサ22等の各種センサの検出情報と、車両のアクセル操作量等の情報を入力し、当該各種情報に基づいて、燃料噴射ノズル3からの燃料噴射量及び燃料噴射時期、電子制御スロットルバルブ6の開度、尿素水インジェクタ14からの尿素水噴射量及び尿素水噴射時期、EGRバルブ17の開度を演算して、上記各種機器の作動制御を行うことで、エンジン2の運転制御を行う。   The engine control unit 30 (nitrogen oxide storage amount estimation unit, purge control unit, temperature rise control unit) includes an input / output device, a storage device (ROM, RAM, nonvolatile RAM, etc.), a timer, and a central processing unit (CPU). Etc., and input detection information of various sensors such as the rotational speed sensor 20, the airflow sensor 21, the selective reduction catalyst temperature sensor 22, and information such as the accelerator operation amount of the vehicle, and based on the various information, The fuel injection amount and fuel injection timing from the fuel injection nozzle 3, the opening degree of the electronic control throttle valve 6, the urea water injection amount and urea water injection timing from the urea water injector 14, and the opening degree of the EGR valve 17 are calculated, Operation control of the engine 2 is performed by performing operation control of the various devices.

また、エンジンコントロールユニット30は、ポスト噴射等により、空燃比を14.7以下のストイキまたはリッチとするとともにNOx吸蔵触媒11を所定温度以上に昇温させることで、NOx吸蔵触媒11に貯留したNOxを還元除去するNOxパージを実行する機能を有している(パージ制御部)。
次に、図2を用いて、NOx吸蔵触媒11に貯留されたNOxを還元除去するNOxパージ制御について説明する。
Further, the engine control unit 30 makes the air-fuel ratio stoichiometric or rich at 14.7 or less by post injection or the like, and raises the NOx storage catalyst 11 to a predetermined temperature or higher, so that the NOx stored in the NOx storage catalyst 11 is increased. It has a function of performing NOx purge for reducing and removing (purge control unit).
Next, NOx purge control for reducing and removing NOx stored in the NOx storage catalyst 11 will be described with reference to FIG.

図2は、エンジンコントロールユニット30におけるNOxパージ制御手順を示すフローチャートである。
図2に示す本実施形態の排気浄化装置1の作動制御は、エンジン運転時にエンジンコントロールユニット30において所定期間毎に繰り返し実行される。
始めに、ステップS10では、NOx吸蔵触媒11に吸蔵されているNOx吸蔵量Qa(窒素酸化物吸蔵量)が所定値A(第1の吸蔵量)より大きいか否かを判別する。NOx吸蔵量Qaは、例えば前回のNOxパージ終了から現在までのエンジン2の運転時間及び運転状態に基づいて推定すればよい(窒素酸化物吸蔵量推定部)。所定値Aは、NOxパージを実行するか否かを判別する閾値であり、NOx吸蔵触媒11におけるNOx吸蔵量Qaの最大許容量より少ない値に設定すればよい。NOx吸蔵量Qaが所定値Aより大きい場合には、ステップS20に進む。NOx吸蔵量Qaが所定値A以下である場合には、本ルーチンを終了する。
FIG. 2 is a flowchart showing a NOx purge control procedure in the engine control unit 30.
The operation control of the exhaust emission control device 1 of this embodiment shown in FIG. 2 is repeatedly executed at predetermined intervals in the engine control unit 30 during engine operation.
First, in step S10, it is determined whether or not the NOx storage amount Qa (nitrogen oxide storage amount) stored in the NOx storage catalyst 11 is greater than a predetermined value A (first storage amount). The NOx occlusion amount Qa may be estimated based on, for example, the operation time and operation state of the engine 2 from the end of the previous NOx purge to the present (nitrogen oxide occlusion amount estimation unit). The predetermined value A is a threshold value for determining whether or not to perform NOx purge, and may be set to a value smaller than the maximum allowable amount of the NOx storage amount Qa in the NOx storage catalyst 11. When the NOx occlusion amount Qa is larger than the predetermined value A, the process proceeds to step S20. When the NOx occlusion amount Qa is equal to or less than the predetermined value A, this routine ends.

ステップS20では、NOx吸蔵量Qaが所定値B(第2の吸蔵量)より大きいか否かを判別する。所定値Bは、所謂スリップ判定値であって、所定値Aより大きい値であり、NOxパージを行った際にNOxが還元除去しきれずにNOx吸蔵触媒11から流出してしまうか否かを判別可能な閾値に設定すればよい。また、第2の吸蔵量を第1の吸蔵量と同じ値に設定してもよい。NOx吸蔵量Qaが所定値Bより大きい場合には、ステップS30に進む。NOx吸蔵量Qaが所定値B以下である場合には、ステップS60に進む。   In step S20, it is determined whether or not the NOx storage amount Qa is greater than a predetermined value B (second storage amount). The predetermined value B is a so-called slip determination value, which is larger than the predetermined value A, and determines whether or not NOx is not completely reduced and removed from the NOx storage catalyst 11 when NOx purge is performed. What is necessary is just to set to the possible threshold value. Further, the second storage amount may be set to the same value as the first storage amount. When the NOx occlusion amount Qa is larger than the predetermined value B, the process proceeds to step S30. When the NOx occlusion amount Qa is equal to or less than the predetermined value B, the process proceeds to step S60.

ステップS30では、選択還元触媒13におけるアンモニア吸着量Qbが所定値Cより大きいか否かを判別する。アンモニア吸着量Qbは、例えば選択還元触媒13におけるアンモニア吸着量Qbの増加分から消費分を減算して求めればよい。アンモニア吸着量Qbの増加分は、尿素水噴射量と排気温度に依存するアンモニア生成率とアンモニア吸着率との積算値により演算できる。なお、アンモニア吸着率は、アンモニア既吸着量が多い場合に低くなり、選択還元触媒13の温度にも依存する。アンモニア吸着量Qbの消費分は、選択還元触媒13入口のNOx量と選択還元触媒13の温度及びアンモニア既吸着量に依存するNOx浄化率との積算値に、選択還元触媒13の温度及びアンモニア既吸着量に依存する選択還元触媒13から脱離または酸化してしまうアンモニア量を加算した値で求められる。所定値Cは、NOxパージした際にNOx吸蔵触媒11から流出して選択還元触媒13に流入するNOxを十分に還元除去できるアンモニア吸着量に設定すればよい。アンモニア吸着量Qbが所定値Cより大きい場合には、ステップS40に進む。アンモニア吸着量Qbが所定値C以下である場合には、ステップS80に進む。   In step S30, it is determined whether or not the ammonia adsorption amount Qb in the selective reduction catalyst 13 is larger than a predetermined value C. The ammonia adsorption amount Qb may be obtained, for example, by subtracting the consumption amount from the increment of the ammonia adsorption amount Qb in the selective reduction catalyst 13. The increase in the ammonia adsorption amount Qb can be calculated from the integrated value of the ammonia production rate and the ammonia adsorption rate depending on the urea water injection amount and the exhaust temperature. Note that the ammonia adsorption rate decreases when the amount of ammonia already adsorbed is large, and also depends on the temperature of the selective reduction catalyst 13. The consumption amount of the ammonia adsorption amount Qb is obtained by adding the NOx amount at the inlet of the selective reduction catalyst 13 to the integrated value of the NOx purification rate depending on the temperature of the selective reduction catalyst 13 and the ammonia preadsorption amount. It is obtained as a value obtained by adding the amount of ammonia desorbed or oxidized from the selective reduction catalyst 13 depending on the amount of adsorption. The predetermined value C may be set to an ammonia adsorption amount that can sufficiently reduce and remove NOx that flows out from the NOx storage catalyst 11 and flows into the selective reduction catalyst 13 when the NOx purge is performed. When the ammonia adsorption amount Qb is larger than the predetermined value C, the process proceeds to step S40. If the ammonia adsorption amount Qb is less than or equal to the predetermined value C, the process proceeds to step S80.

ステップS40では、選択還元触媒温度センサ22から選択還元触媒温度Tbを入力し、選択還元触媒温度Tbが所定値T1(所定温度)より低いか否かを判別する。所定値T1は、選択還元触媒13においてNOxを十分に還元除去可能となる活性温度に設定すればよい。選択還元触媒温度Tbが所定値T1より低い場合には、ステップS50に進む。選択還元触媒温度Tbが所定値T1以上である場合には、ステップS60に進む。   In step S40, the selective reduction catalyst temperature Tb is input from the selective reduction catalyst temperature sensor 22, and it is determined whether or not the selective reduction catalyst temperature Tb is lower than a predetermined value T1 (predetermined temperature). The predetermined value T1 may be set to an activation temperature at which NOx can be sufficiently reduced and removed in the selective reduction catalyst 13. When the selective reduction catalyst temperature Tb is lower than the predetermined value T1, the process proceeds to step S50. When the selective reduction catalyst temperature Tb is equal to or higher than the predetermined value T1, the process proceeds to step S60.

ステップS50では、選択還元触媒活性用昇温制御(昇温制御)を実行する(昇温制御部)。選択還元触媒活性用昇温制御は、電子制御スロットルバルブ6によって吸気量を絞ったり、燃料噴射ノズル3からの燃料噴射量を増加したりすることで、排気温度を上昇させる。なお、ここでは、NOx吸蔵触媒11からNOxが流出しないように、排気の空燃比をNOxパージの際よりもリーン側に制御する。例えば、本実施形態のエンジン2が通常燃焼時に空燃比20程度のリーンバーンエンジンである場合には、NOxパージ時には空燃比14.7以下のストイキまたはリッチ燃焼とし、本ステップの選択還元触媒活性用昇温制御及び後述するステップS90におけるアンモニア発生用昇温制御では、空燃比を17〜18程度のスライトリーンにすればよい。すなわち、通常のリーン燃焼よりリッチ側には空燃比を変更するものの、空燃比としては14.7以上のリーン燃焼を実施するものである。これにより、NOxの流出増加を抑えつつ選択還元触媒13を昇温することが可能となる。なお、このようにスライトリーンにしてもNOxの流出が抑えられるのは、NOx吸蔵触媒に吸蔵されたNOxは硝酸塩(硝酸バリウムなど)として蓄積されることから、硝酸塩を分解してNOxを放出するには還元雰囲気にする必要があるため、スライトリーンではNOx は放出されないからである。そして、ステップS60に進む。   In step S50, the selective reduction catalyst activation temperature increase control (temperature increase control) is executed (temperature increase control unit). The temperature increase control for selective reduction catalyst activation raises the exhaust temperature by reducing the intake air amount by the electronically controlled throttle valve 6 or increasing the fuel injection amount from the fuel injection nozzle 3. Here, the air-fuel ratio of the exhaust gas is controlled to be leaner than the NOx purge so that NOx does not flow out from the NOx storage catalyst 11. For example, when the engine 2 of the present embodiment is a lean burn engine having an air-fuel ratio of about 20 during normal combustion, stoichiometric or rich combustion with an air-fuel ratio of 14.7 or less is performed during NOx purge, and the selective reduction catalyst activity for this step is used. In the temperature increase control and the ammonia generation temperature increase control in step S90, which will be described later, the air-fuel ratio may be set to about 17-18. That is, although the air-fuel ratio is changed to a richer side than normal lean combustion, lean combustion with an air-fuel ratio of 14.7 or more is performed. Thereby, it is possible to raise the temperature of the selective reduction catalyst 13 while suppressing an increase in the outflow of NOx. In addition, the NOx outflow can be suppressed even in such a light lean manner because the NOx stored in the NOx storage catalyst is accumulated as nitrates (such as barium nitrate), so the nitrates are decomposed and NOx is released. This is because NOx is not released in light lean because it is necessary to have a reducing atmosphere. Then, the process proceeds to step S60.

ステップS60では、NOxパージ条件が成立しているか否かを判別する。NOxパージ条件は、例えばNOx吸蔵触媒11の温度がNOxパージ可能な所定温度(第1の所定温度)以上であることを検出したり、高負荷運転であることを判定したりすればよい。NOxパージ条件が成立している場合には、ステップS70に進む。NOxパージ条件が成立していない場合には、本ルーチンを終了する。   In step S60, it is determined whether or not a NOx purge condition is satisfied. The NOx purge condition may be determined, for example, by detecting that the temperature of the NOx occlusion catalyst 11 is equal to or higher than a predetermined temperature (first predetermined temperature) at which NOx purging is possible, or determining that the operation is a high load operation. If the NOx purge condition is satisfied, the process proceeds to step S70. If the NOx purge condition is not satisfied, this routine is terminated.

ステップS70では、NOxパージ(パージ制御)を実行する。NOxパージは、上記のように、ポスト噴射等により、NOx吸蔵触媒11をパージ可能な第1の所定温度以上に維持しつつ空燃比を14.7以下のストイキまたはリッチとすることで行なわれる。そして、本ルーチンを終了する。
ステップS80では、選択還元触媒温度センサ22から選択還元触媒温度Tbを入力し、選択還元触媒温度Tbが所定値T2より低いか否かを判別する。所定値T2は、尿素水が加水分解されてアンモニアが発生する温度に設定すればよい。選択還元触媒温度Tbが所定値T2より低い場合には、ステップS90に進む。選択還元触媒温度Tbが所定値T2以上である場合には、ステップS100に進む。
In step S70, NOx purge (purge control) is executed. As described above, the NOx purge is performed by maintaining the NOx storage catalyst 11 at or above the first predetermined temperature at which purging is possible by post-injection or the like and making the air-fuel ratio stoichiometric or rich below 14.7. Then, this routine ends.
In step S80, the selective reduction catalyst temperature Tb is input from the selective reduction catalyst temperature sensor 22, and it is determined whether or not the selective reduction catalyst temperature Tb is lower than a predetermined value T2. The predetermined value T2 may be set to a temperature at which urea water is hydrolyzed and ammonia is generated. When the selective reduction catalyst temperature Tb is lower than the predetermined value T2, the process proceeds to step S90. When the selective reduction catalyst temperature Tb is equal to or higher than the predetermined value T2, the process proceeds to step S100.

ステップS90では、アンモニア発生用昇温制御を実行する。アンモニア発生用昇温制御は、尿素水インジェクタ14から噴射した尿素水を加水分解してアンモニアを発生させ、選択還元触媒13に吸着させるための制御であり、ステップS50における選択還元触媒活性用昇温制御と同様に、吸気量を絞ったり、燃料噴射量を増加したりすることで、排気温度を上昇させる。そして、ステップS100に進む。   In step S90, the temperature increase control for ammonia generation is executed. The temperature increase control for ammonia generation is control for hydrolyzing the urea water injected from the urea water injector 14 to generate ammonia and adsorb it to the selective reduction catalyst 13, and the temperature increase for selective reduction catalyst activity in step S50. Similar to the control, the exhaust gas temperature is raised by reducing the intake air amount or increasing the fuel injection amount. Then, the process proceeds to step S100.

ステップS100では、尿素水インジェクタ14から、選択還元触媒13においてNOxを還元除去するための尿素水を噴射させる。そして、ステップS30に戻る。
以上のように、本実施形態では、排気通路10に低温領域で浄化性能の優れたNOx吸蔵触媒11と高温領域で浄化性能の優れた選択還元触媒13を備えているので、広範囲の排気温度でNOxの浄化性能を向上させることができる。NOx吸蔵触媒11にNOxが所定値Aを超えて多く吸蔵された場合には、NOxパージが要求されるが、例えばアイドリング運転のような低負荷運転が継続されてNOx吸蔵触媒11の温度が低下し、NOxパージが不能である場合には、NOx吸蔵触媒11におけるNOx吸蔵量Qaが更に増加する。本実施形態では、NOxの発生を抑える装置としてEGR装置15を備えているが、アイドリング運転のような運転状況では燃焼安定性を確保するため、排気の還流量が抑えられ、NOxの発生を十分に抑制することが困難である。
In step S <b> 100, urea water for reducing and removing NOx in the selective reduction catalyst 13 is injected from the urea water injector 14. Then, the process returns to step S30.
As described above, in the present embodiment, the exhaust passage 10 includes the NOx storage catalyst 11 having excellent purification performance in the low temperature region and the selective reduction catalyst 13 having excellent purification performance in the high temperature region. The NOx purification performance can be improved. When the NOx storage catalyst 11 stores a large amount of NOx exceeding the predetermined value A, a NOx purge is required. For example, a low load operation such as an idling operation is continued, and the temperature of the NOx storage catalyst 11 decreases. When NOx purge is impossible, the NOx occlusion amount Qa in the NOx occlusion catalyst 11 further increases. In the present embodiment, the EGR device 15 is provided as a device that suppresses the generation of NOx. However, in order to ensure combustion stability in an operating situation such as an idling operation, the exhaust gas recirculation amount is suppressed, and the generation of NOx is sufficient. It is difficult to suppress.

そこで、本実施形態では、NOx吸蔵触媒11におけるNOx吸蔵量Qaがスリップ判定値である所定値Bより大きくなってしまった場合に選択還元触媒活性用昇温制御を行うことで、排気温度を上昇させて選択還元触媒13の温度を活性温度である所定値T1まで上昇させる。これにより、NOx吸蔵触媒11からNOxが流出したとしても、NOx吸蔵触媒11の下流の選択還元触媒13によって浄化することができ、大気中へのNOxの排出を減少させることができる。また、この昇温制御では空燃比をリーンに留めておくことで、燃料消費を抑えることができる。   Therefore, in the present embodiment, when the NOx occlusion amount Qa in the NOx occlusion catalyst 11 becomes larger than the predetermined value B which is the slip determination value, the exhaust gas temperature is raised by performing the temperature reduction control for selective reduction catalyst activation. Thus, the temperature of the selective reduction catalyst 13 is raised to a predetermined value T1, which is the activation temperature. Thereby, even if NOx flows out from the NOx storage catalyst 11, it can be purified by the selective reduction catalyst 13 downstream of the NOx storage catalyst 11, and the discharge of NOx into the atmosphere can be reduced. In this temperature increase control, fuel consumption can be suppressed by keeping the air-fuel ratio lean.

また、NOx吸蔵触媒11におけるNOx吸蔵量Qaが所定値Bより大きく、かつ選択還元触媒13のアンモニア吸着量Qbが所定値Cに達していない場合には、アンモニア発生用昇温制御を行って尿素が加水分解できる温度まで選択還元触媒13を昇温させた上で尿素水を噴射しておくことで、選択還元触媒13を十分に活性化させておくだけでなく選択還元触媒13のアンモニア吸着量Qbを十分に確保しておくことができる。   Further, when the NOx occlusion amount Qa in the NOx occlusion catalyst 11 is larger than the predetermined value B and the ammonia adsorption amount Qb of the selective reduction catalyst 13 has not reached the predetermined value C, the temperature rise control for ammonia generation is performed to increase the urea. The selective reduction catalyst 13 is heated to a temperature at which it can be hydrolyzed, and urea water is injected, so that the selective reduction catalyst 13 is not only sufficiently activated but also the ammonia adsorption amount of the selective reduction catalyst 13. Qb can be secured sufficiently.

以上のように、本実施形態では、NOx吸蔵量Qaが所定値Aを超えてNOxパージが要求されている状態において、NOx吸蔵触媒11におけるNOx吸蔵量Qaがスリップ判定値より大きくなった場合には、NOxパージから昇温制御(昇温制御、アンモニア発生用昇温制御)に切換えて行うことで、NOxパージが不能であるときに選択還元触媒13にアンモニアを十分に吸着させるとともに十分に活性化させておき、選択還元触媒13においてNOxの浄化を可能に準備させておくことができる。したがって、例えば高負荷運転が行なわれてNOxパージが可能となったときに、NOxパージの開始時においてNOx吸蔵触媒11からNOxが流出したとしても選択還元触媒13によってすぐにかつ十分に浄化することができ、大気中へのNOxの排出を減少させ、排気浄化性能を向上させることができる。また、これらの昇温制御によりNOx吸蔵触媒11も昇温するので、NOxパージの開始を早めることができる。   As described above, in the present embodiment, when the NOx storage amount Qa exceeds the predetermined value A and the NOx purge is requested, the NOx storage amount Qa in the NOx storage catalyst 11 becomes larger than the slip determination value. Is switched from NOx purge to temperature increase control (temperature increase control, ammonia generation temperature increase control), so that when the NOx purge is impossible, the selective reduction catalyst 13 is sufficiently adsorbed and sufficiently activated. The selective reduction catalyst 13 can be prepared so as to be able to purify NOx. Therefore, for example, when NOx purge becomes possible due to high load operation, even if NOx flows out from the NOx storage catalyst 11 at the start of the NOx purge, it is immediately and sufficiently purified by the selective reduction catalyst 13. It is possible to reduce NOx emission into the atmosphere and improve exhaust purification performance. In addition, since the temperature of the NOx storage catalyst 11 is also raised by these temperature rise controls, the start of the NOx purge can be accelerated.

なお、以上の実施形態では、NOx吸蔵触媒11におけるNOx吸蔵量Qaがスリップ判定値である所定値Bより大きくなった際に昇温制御を行うが、NOx吸蔵量が所定値B以下であり通常燃焼である場合でも、エンジン2の負荷が所定値以上の高負荷運転状態である場合には、図2に示す作動制御のステップS30以降を実施するようにしてもよい。この所定値は、NOx吸蔵触媒11が高温となってNOxが流出するような運転状態での負荷である。   In the above embodiment, the temperature rise control is performed when the NOx occlusion amount Qa in the NOx occlusion catalyst 11 becomes larger than the predetermined value B which is the slip determination value, but the NOx occlusion amount is less than the predetermined value B and is normal. Even in the case of combustion, when the load of the engine 2 is in a high-load operation state of a predetermined value or more, the operation control step S30 and subsequent steps shown in FIG. This predetermined value is a load in an operating state in which the NOx storage catalyst 11 becomes hot and NOx flows out.

このように、高負荷運転においても選択還元触媒13の昇温制御を行うことで、NOx吸蔵触媒11のNOxの浄化率が低下してNOx吸蔵触媒11からNOxが流出する高温下においても、NOx吸蔵触媒11の下流の選択還元触媒13において十分にNOxを除去することができ、大気中へのNOxの排出を抑制することができる。
また、本願発明は、上記実施形態に限定するものではない。本願発明は、排気浄化装置として排気通路にNOx吸蔵触媒及び選択還元触媒を備えたエンジンに広く適用することができる。
In this way, by controlling the temperature increase of the selective reduction catalyst 13 even in a high load operation, the NOx purification rate of the NOx storage catalyst 11 is reduced, and even at high temperatures where NOx flows out of the NOx storage catalyst 11, NOx. NOx can be sufficiently removed in the selective reduction catalyst 13 downstream of the storage catalyst 11, and the emission of NOx into the atmosphere can be suppressed.
The present invention is not limited to the above embodiment. The present invention can be widely applied to an engine having an NOx storage catalyst and a selective reduction catalyst in an exhaust passage as an exhaust purification device.

2 エンジン
10 排気通路
11 NOx吸蔵触媒(窒素酸化物吸蔵還元触媒)
13 選択還元触媒
14 尿素水インジェクタ(還元剤供給部)
30 エンジンコントロールユニット(窒素酸化物吸蔵量推定部、パージ制御部、昇温制御部)
2 Engine 10 Exhaust passage 11 NOx storage catalyst (nitrogen oxide storage reduction catalyst)
13 Selective reduction catalyst 14 Urea water injector (reducing agent supply unit)
30 Engine control unit (nitrogen oxide storage amount estimation unit, purge control unit, temperature rise control unit)

Claims (5)

エンジンの排気通路に設けられ、排気中の窒素酸化物を吸蔵する窒素酸化物吸蔵還元触媒と、
前記窒素酸化物吸蔵還元触媒の下流側の前記排気通路に設けられ、還元剤を用いて窒素酸化物を還元除去する選択還元触媒と、
前記選択還元触媒に前記還元剤を供給する還元剤供給部と、
前記窒素酸化物吸蔵還元触媒の窒素酸化物吸蔵量を推定する窒素酸化物吸蔵量推定部と、
前記窒素酸化物吸蔵量が所定の第1の吸蔵量より大きくなった状態で、所定のパージ条件が成立した場合には、排気の空燃比をストイキまたはリッチにして、前記窒素酸化物吸蔵還元触媒に吸蔵した前記窒素酸化物を還元するパージ制御を実行するパージ制御部と、
前記窒素酸化物吸蔵量が前記第1の吸蔵量より大きくなった状態で、前記パージ条件が成立しない場合には、排気の空燃比をリーンにした状態で、前記還元剤供給部により前記還元剤を供給して前記選択還元触媒に前記還元剤を供給させるとともに前記選択還元触媒の温度を所定温度以上に上昇させる昇温制御を実行する昇温制御部と、
を備えることを特徴とするエンジンの排気浄化装置。
A nitrogen oxide storage reduction catalyst that is provided in the exhaust passage of the engine and stores the nitrogen oxide in the exhaust;
A selective reduction catalyst that is provided in the exhaust passage on the downstream side of the nitrogen oxide storage reduction catalyst and that reduces and removes nitrogen oxide using a reducing agent;
A reducing agent supply unit for supplying the reducing agent to the selective reduction catalyst;
A nitrogen oxide storage amount estimation unit for estimating the nitrogen oxide storage amount of the nitrogen oxide storage reduction catalyst;
When a predetermined purge condition is satisfied in a state where the nitrogen oxide storage amount is larger than the predetermined first storage amount, the exhaust gas air-fuel ratio is stoichiometric or rich, and the nitrogen oxide storage reduction catalyst A purge control unit for performing purge control to reduce the nitrogen oxides occluded in
If the purge condition is not satisfied when the nitrogen oxide storage amount is larger than the first storage amount, the reducing agent supply unit causes the reducing agent supply unit to make the reducing agent in a lean state. And a temperature increase control unit for performing temperature increase control for supplying the reducing agent to the selective reduction catalyst and increasing the temperature of the selective reduction catalyst to a predetermined temperature or higher,
An exhaust emission control device for an engine comprising:
前記パージ制御部は、前記昇温制御を実行中に前記パージ条件が成立した際には、前記昇温制御から前記パージ制御に強制的に切換えることを特徴とする請求項1に記載のエンジンの排気浄化装置。   2. The engine according to claim 1, wherein the purge control unit forcibly switches from the temperature increase control to the purge control when the purge condition is satisfied during execution of the temperature increase control. Exhaust purification device. 前記昇温制御は、前記エンジンの吸気量の絞り及び前記エンジンの燃料噴射量の増加の少なくともいずれか一方により行われることを特徴とする請求項1または2に記載のエンジンの排気浄化装置。   3. The engine exhaust purification device according to claim 1, wherein the temperature increase control is performed by at least one of a restriction of an intake amount of the engine and an increase of a fuel injection amount of the engine. 前記還元剤供給部は、前記選択還元触媒の上流側の前記排気通路に尿素水溶液を供給して、当該尿素水溶液が加水分解して得られるアンモニアを前記選択還元触媒に供給することを特徴とする請求項1から3のいずれかに記載のエンジンの排気浄化装置。   The reducing agent supply unit supplies an aqueous urea solution to the exhaust passage on the upstream side of the selective reduction catalyst, and supplies ammonia obtained by hydrolysis of the aqueous urea solution to the selective reduction catalyst. The exhaust emission control device for an engine according to any one of claims 1 to 3. 前記エンジンの負荷が所定値以上である場合には、前記窒素酸化物吸蔵量に拘わらず、前記昇温制御を実行することを特徴とする請求項1から4のいずれかに記載のエンジンの排気浄化装置。   The engine exhaust according to any one of claims 1 to 4, wherein when the engine load is equal to or greater than a predetermined value, the temperature increase control is executed regardless of the nitrogen oxide storage amount. Purification equipment.
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