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JP2002097940A - Operating method of exhaust gas purification device - Google Patents

Operating method of exhaust gas purification device

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Publication number
JP2002097940A
JP2002097940A JP2000294052A JP2000294052A JP2002097940A JP 2002097940 A JP2002097940 A JP 2002097940A JP 2000294052 A JP2000294052 A JP 2000294052A JP 2000294052 A JP2000294052 A JP 2000294052A JP 2002097940 A JP2002097940 A JP 2002097940A
Authority
JP
Japan
Prior art keywords
reduction catalyst
exhaust gas
nox storage
nox
storage reduction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2000294052A
Other languages
Japanese (ja)
Other versions
JP3545691B2 (en
Inventor
Mitsuru Hosoya
満 細谷
Hiroshi Hirabayashi
浩 平林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hino Motors Ltd
Original Assignee
Hino Motors Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hino Motors Ltd filed Critical Hino Motors Ltd
Priority to JP2000294052A priority Critical patent/JP3545691B2/en
Publication of JP2002097940A publication Critical patent/JP2002097940A/en
Application granted granted Critical
Publication of JP3545691B2 publication Critical patent/JP3545691B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【課題】 ディーゼルエンジンの排気ガスをNOx吸蔵
還元触媒で浄化するにあたり、該NOx吸蔵還元触媒の
硫酸塩による被毒をディーゼルエンジン側の運転制御を
行わずに解消し得るようにする。 【解決手段】 ディーゼルエンジン1からの排気ガス7
が流通する排気管9の途中にNOx吸蔵還元触媒11を
装備し、該NOx吸蔵還元触媒11に対し還元剤10を
適宜に添加し且つ前記NOx吸蔵還元触媒11を適宜に
迂回させて排気ガス7を流し得るように構成した排気浄
化装置の運転方法に関し、定期的にNOx吸蔵還元触媒
11に排気ガス7を流しつつ還元剤10を添加して該N
Ox吸蔵還元触媒11を所定温度以上に昇温させ且つそ
の直後にNOx吸蔵還元触媒11を迂回させて排気ガス
7を流しながらNOx吸蔵還元触媒11に再び還元剤1
0を添加して脱硫処理を施す。
(57) Abstract: In purifying exhaust gas of a diesel engine with a NOx storage reduction catalyst, it is possible to eliminate poisoning of the NOx storage reduction catalyst by sulfate without performing operation control on the diesel engine side. To SOLUTION: Exhaust gas 7 from a diesel engine 1
A NOx storage-reduction catalyst 11 is provided in the exhaust pipe 9 through which the NOx storage-reduction catalyst 11 is added. The reducing agent 10 is appropriately added to the NOx storage-reduction catalyst 11, and the exhaust gas 7 With respect to an operation method of an exhaust gas purifying apparatus configured to flow N 2, the reducing agent 10 is added by periodically adding the reducing agent 10 while flowing the exhaust gas 7 to the NOx storage reduction catalyst 11.
The temperature of the Ox storage reduction catalyst 11 is raised to a predetermined temperature or higher, and immediately thereafter, the NOx storage reduction catalyst 11 is bypassed and the reducing agent 1 is again supplied to the NOx storage reduction catalyst 11 while flowing the exhaust gas 7.
0 is added to perform desulfurization treatment.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ディーゼルエンジ
ンに用いる排気浄化装置の運転方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for operating an exhaust emission control device used for a diesel engine.

【0002】[0002]

【従来の技術】従来より、ディーゼルエンジンにおいて
は、排気ガスが流通する排気管の途中にNOx還元触媒
を装備し、該NOx還元触媒の上流側に必要量の還元剤
を添加して該還元剤をNOx還元触媒上で排気ガス中の
NOx(窒素酸化物)と還元反応させることによりNOx
の排出濃度を低減し得るようにしたものがある。
2. Description of the Related Art Conventionally, in a diesel engine, a NOx reduction catalyst is provided in an exhaust pipe through which exhaust gas flows, and a required amount of a reducing agent is added upstream of the NOx reducing catalyst to reduce the amount of the reducing agent. Is reduced on the NOx reduction catalyst with NOx (nitrogen oxide) in the exhaust gas to produce NOx.
Some of them are capable of reducing the emission concentration of methane.

【0003】他方、理論空燃比より大きな空燃比で希薄
燃焼(リーンバーン)を行わせることにより大幅な燃費
の向上を図り得ることが広く知られているが、このよう
な希薄燃焼運転を行うことを想定したディーゼルエンジ
ンに関してもNOxの排出濃度を低減することは重要な
課題となっている。
[0003] On the other hand, it is widely known that a lean burn can be performed at a higher air-fuel ratio than the stoichiometric air-fuel ratio to greatly improve fuel efficiency. It is also an important issue to reduce the NOx emission concentration for a diesel engine that assumes the following.

【0004】しかしながら、一般的に、希薄燃焼運転時
における酸素過剰存在下では、NOx還元触媒上におい
て、還元剤がNOxと反応するよりも先に酸素と反応し
てしまうので、希薄燃焼運転時における実用化レベルの
高いNOx低減効果を得ることが難しかった。
[0004] However, in general, in the presence of excess oxygen during the lean burn operation, the reducing agent reacts with oxygen on the NOx reduction catalyst before reacting with NOx. It was difficult to obtain a high NOx reduction effect at a practical level.

【0005】そこで、希薄燃焼運転時においてもNOx
を低減し得る触媒として、排気ガス中の酸素濃度が高い
希薄燃焼運転時にNOxを酸化して硝酸塩の状態で一時
的に吸蔵し且つ排気ガス中の酸素濃度が低い理論空燃比
運転時に還元剤の介在によりNOxを分解放出して還元
浄化する性質を備えたNOx吸蔵還元触媒の実用化が現
在検討されている。
Therefore, even during lean burn operation, NOx
As a catalyst that can reduce NOx, NOx is oxidized during lean burn operation in which the oxygen concentration in the exhaust gas is high to temporarily store NOx in the state of nitrate, and the reducing agent is used during stoichiometric air-fuel ratio operation in which the oxygen concentration in the exhaust gas is low. At present, practical use of a NOx storage reduction catalyst having a property of decomposing and releasing NOx to reduce and purify is being studied.

【0006】例えば、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・アルミナ触媒など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。
For example, as this type of NOx storage reduction catalyst, a platinum-barium-alumina catalyst, an iridium-
Platinum / barium / alumina catalysts are already known as having the above-mentioned properties.

【0007】ただし、NOx吸蔵還元触媒に吸蔵された
NOxを放出させて該NOx吸蔵還元触媒の再生を図るの
に際し、いちいち運転状態を希薄燃焼運転から理論空燃
比運転に切り替えていたのでは、せっかくの希薄燃焼運
転による燃費向上のメリットが損なわれてしまうため、
希薄燃焼運転としたままでNOx吸蔵還元触媒の良好な
再生を図り得るようにすることが望まれているが、希薄
燃焼運転時における酸素過剰存在下では、排気ガス中の
酸素濃度が高いために、前述したNOx還元触媒の場合
と同様に、HCなどの還元剤がNOxと反応するよりも
先に酸素と反応して消費されてしまい、これにより還元
剤とNOxの反応選択性が低下してNOx吸蔵還元触媒の
良好な再生を図ることができないという問題があった。
However, when the NOx stored in the NOx storage reduction catalyst is released to regenerate the NOx storage reduction catalyst, the operating state must be switched from lean combustion operation to stoichiometric air-fuel ratio operation. The advantage of improved fuel economy by lean burn operation is lost,
It is desired to be able to achieve good regeneration of the NOx storage reduction catalyst while maintaining the lean burn operation. However, in the presence of excess oxygen during the lean burn operation, the oxygen concentration in the exhaust gas is high. As in the case of the above-described NOx reduction catalyst, the reducing agent such as HC reacts with oxygen before being reacted with NOx and is consumed, whereby the reaction selectivity between the reducing agent and NOx is reduced. There was a problem that good regeneration of the NOx storage reduction catalyst could not be achieved.

【0008】そこで、本発明者らは、排気管の途中にN
Ox吸蔵還元触媒を装備した上、該NOx吸蔵還元触媒を
迂回するようにバイパス流路を付設し、このバイパス流
路側に排気ガスを切り替えて流しながら還元剤の添加を
行い、該還元剤の添加量に対する相対的な空気過剰率を
下げて還元剤とNOxの反応選択性を向上し、これによ
りNOx吸蔵還元触媒からNOxを積極的に分解放出させ
て該NOx吸蔵還元触媒の良好な再生を図り、その放出
したNOxをNOx吸蔵還元触媒上で前記還元剤と反応さ
せて還元浄化させることを創案するに到り、これを特願
平11−328339号として既に出願している。
Therefore, the present inventors have found that N
In addition to the provision of the Ox storage reduction catalyst, a bypass flow path is provided so as to bypass the NOx storage reduction catalyst, and the reducing agent is added while switching the exhaust gas to the bypass flow path side to add the reducing agent. By reducing the relative excess ratio of air to the amount, the reaction selectivity between the reducing agent and NOx is improved, whereby NOx is actively decomposed and released from the NOx storage-reduction catalyst to achieve good regeneration of the NOx storage-reduction catalyst. The inventors have come up with the idea of reacting the released NOx with the reducing agent on a NOx storage-reduction catalyst to purify the NOx, which has already been filed as Japanese Patent Application No. 11-328339.

【0009】[0009]

【発明が解決しようとする課題】しかしながら、ディー
ゼルエンジンの排気ガス中には、燃料中の硫黄分に由来
するSO2が存在するため、このSO2がNOx吸蔵還元
触媒上でNOxと同様に酸化して硫酸塩となってしまう
という不具合があり、この硫酸塩が硝酸塩と比べて安定
であることからNOx吸蔵還元触媒が硫酸塩により被毒
劣化し、これによりNOxの吸蔵が不可能となってNOx
浄化率が低下するという問題に関しては未だ具体的な実
用レベルの解決策が提案されていないのが実情である。
However, since SO 2 derived from sulfur in the fuel is present in the exhaust gas of a diesel engine, this SO 2 is oxidized on the NOx storage reduction catalyst in the same manner as NOx. The sulfate is more stable than the nitrate, and the NOx storage reduction catalyst is poisoned and deteriorated by the sulfate, which makes it impossible to store NOx. NOx
As for the problem that the purification rate decreases, there is no actual solution at the practical level.

【0010】ただし、硫酸塩による被毒を解消する手法
自体は、理論空燃比より小さな空燃比でリッチ燃焼を行
わせ且つ約600℃以上の高温雰囲気に保つことによ
り、NOx吸蔵還元触媒からSO2を放出させてNOx吸
蔵還元触媒の再生を図ることが知られているが、これを
ディーゼルエンジン側の運転制御で実現することは、黒
煙の発生が不可避となってしまう運転領域でディーゼル
エンジンを運転することを意味しているので、このよう
な黒煙の発生を回避しつつディーゼルエンジン側の運転
制御でNOx吸蔵還元触媒の脱硫処理の条件を整えるこ
とは現実的に難しいことであった。
However, the method itself for eliminating poisoning by sulfate is to perform rich combustion at an air-fuel ratio smaller than the stoichiometric air-fuel ratio and to maintain the atmosphere at a high temperature of about 600 ° C. or higher, so that the SO 2 from the NOx storage reduction catalyst can be reduced. It is known that the NOx storage reduction catalyst is regenerated by releasing the NOx. However, realizing this by operation control on the diesel engine side requires the diesel engine to operate in an operation region where black smoke is inevitable. This means that it is practically difficult to adjust the conditions for the desulfurization treatment of the NOx storage reduction catalyst by the operation control on the diesel engine side while avoiding the generation of such black smoke.

【0011】本発明は、上述の実情に鑑みてなされたも
のであり、ディーゼルエンジンの排気ガスをNOx吸蔵
還元触媒で浄化するにあたり、該NOx吸蔵還元触媒の
硫酸塩による被毒をディーゼルエンジン側の運転制御を
行わずに解消し得るようにすることを目的としている。
The present invention has been made in view of the above-mentioned circumstances, and in purifying exhaust gas of a diesel engine with a NOx storage reduction catalyst, poisoning of the NOx storage reduction catalyst by sulfate on the diesel engine side is performed. It is an object of the present invention to be able to solve the problem without performing operation control.

【0012】[0012]

【課題を解決するための手段】本発明は、ディーゼルエ
ンジンからの排気ガスが流通する排気管の途中に、排気
ガス中の酸素濃度が高い時にNOxを酸化して硝酸塩の
状態で一時的に吸蔵し且つ排気ガス中の酸素濃度が低い
時に還元剤の介在によりNOxを分解放出して還元浄化
するNOx吸蔵還元触媒を装備し、該NOx吸蔵還元触媒
に対し還元剤を適宜に添加し且つ前記NOx吸蔵還元触
媒を適宜に迂回させて排気ガスを流し得るように構成し
た排気浄化装置の運転方法であって、通常はディーゼル
エンジンの排気ガスをNOx吸蔵還元触媒に流し、これ
により排気ガス中のNOxをNOx吸蔵還元触媒に吸蔵さ
せてNOxの低減化を図る一方、定期的に排気ガスをN
Ox吸蔵還元触媒を迂回させて流しながら該NOx吸蔵還
元触媒に還元剤を添加し、これによりNOx吸蔵還元触
媒からNOxを積極的に分解放出させてNOx吸蔵還元触
媒の再生を図り、更には、定期的にNOx吸蔵還元触媒
に排気ガスを流しつつ還元剤を添加してNOx吸蔵還元
触媒を所定温度以上に昇温させ且つその直後にNOx吸
蔵還元触媒を迂回させて排気ガスを流しながら該NOx
吸蔵還元触媒に再び還元剤を添加して脱硫処理を施すこ
とを特徴とするものである。
SUMMARY OF THE INVENTION The present invention oxidizes NOx in the exhaust pipe through which exhaust gas from a diesel engine flows when the oxygen concentration in the exhaust gas is high, and temporarily stores NOx in the state of nitrate. And a NOx storage reduction catalyst that decomposes and releases NOx through the use of a reducing agent when the oxygen concentration in the exhaust gas is low to reduce and purify the NOx. The reducing agent is appropriately added to the NOx storage reduction catalyst, and the NOx An operation method of an exhaust gas purification device configured to allow exhaust gas to flow by appropriately bypassing a storage reduction catalyst, and in which exhaust gas of a diesel engine is normally passed to a NOx storage reduction catalyst, whereby NOx in the exhaust gas is reduced. Is stored in the NOx storage reduction catalyst to reduce NOx.
A reducing agent is added to the NOx storage-reduction catalyst while flowing around the Ox storage-reduction catalyst, thereby actively decomposing and releasing NOx from the NOx storage-reduction catalyst to regenerate the NOx storage-reduction catalyst. A reducing agent is added while flowing exhaust gas to the NOx storage reduction catalyst periodically to raise the temperature of the NOx storage reduction catalyst to a predetermined temperature or higher, and immediately after that, the NOx storage reduction catalyst is bypassed and exhausted by flowing the exhaust gas.
It is characterized in that a reducing agent is added again to the storage reduction catalyst to perform a desulfurization treatment.

【0013】而して、ディーゼルエンジンの酸素濃度の
高い排気ガスをNOx吸蔵還元触媒に流すと、排気ガス
中のNOxがNOx吸蔵還元触媒に硝酸塩の状態で吸蔵さ
れ、これによりディーゼルエンジンの運転時における良
好なNOxの低減化が図られることになる。
When exhaust gas having a high oxygen concentration of the diesel engine is passed through the NOx storage reduction catalyst, NOx in the exhaust gas is stored in the NOx storage reduction catalyst in the form of nitrate, thereby allowing the diesel engine to operate during operation. , A good reduction of NOx is achieved.

【0014】また、定期的にNOx吸蔵還元触媒を迂回
させて排気ガスを流しながらNOx吸蔵還元触媒に還元
剤を添加すると、該還元剤の添加量に対する相対的な空
気過剰率が低下して還元剤とNOxの反応選択性が向上
し、これによりNOx吸蔵還元触媒からNOxを積極的に
分解放出させて該NOx吸蔵還元触媒の良好な再生を図
り、その放出したNOxをNOx吸蔵還元触媒上で前記還
元剤と反応させて良好に還元浄化させることが可能とな
る。
Further, when a reducing agent is added to the NOx storage reduction catalyst while exhaust gas is flowed around the NOx storage reduction catalyst periodically, the relative excess amount of air relative to the amount of the reducing agent is reduced and the reduction is performed. The selectivity of the reaction between the NOx storage and reduction catalyst and the NOx is improved, whereby the NOx storage and reduction catalyst is actively decomposed and released to achieve good regeneration of the NOx storage and reduction catalyst, and the released NOx is transferred to the NOx storage and reduction catalyst. By reacting with the reducing agent, reduction and purification can be performed well.

【0015】更には、NOx吸蔵還元触媒に排気ガスを
流しつつ還元剤を添加すると、排気ガスが流通している
酸素濃度の高い高温雰囲気下での還元剤の酸化反応によ
る発熱でNOx吸蔵還元触媒が所定温度以上に昇温し、
その直後にNOx吸蔵還元触媒を迂回させて排気ガスを
流しながら該NOx吸蔵還元触媒に再び還元剤を添加す
ると、該還元剤の添加量に対する相対的な空気過剰率が
低下して理論空燃比より小さな空燃比のリッチ雰囲気が
実現されるので、NOx吸蔵還元触媒からSO2を放出せ
るための条件がディーゼルエンジン側の運転制御を行わ
ずに整うことになり、NOx吸蔵還元触媒が効率良く脱
硫処理されて硫酸塩による被毒が解消されることにな
る。
Further, when the reducing agent is added while flowing the exhaust gas to the NOx storing and reducing catalyst, the NOx storing and reducing catalyst generates heat due to an oxidation reaction of the reducing agent in a high-temperature atmosphere having a high oxygen concentration in which the exhaust gas flows. Rises above a predetermined temperature,
Immediately after that, when the reducing agent is added again to the NOx storage-reduction catalyst while flowing the exhaust gas while bypassing the NOx storage-reduction catalyst, the relative excess air ratio with respect to the added amount of the reducing agent decreases, and the relative air-fuel ratio becomes lower than the stoichiometric air-fuel ratio. Since a rich atmosphere with a small air-fuel ratio is realized, the conditions for releasing SO 2 from the NOx storage reduction catalyst are set without performing operation control on the diesel engine side, and the NOx storage reduction catalyst is efficiently desulfurized. As a result, the poisoning by the sulfate is eliminated.

【0016】[0016]

【発明の実施の形態】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.

【0017】図1は本発明を実施する形態の一例を示す
もので、図中1はディーゼルエンジンを示し、ここに図
示しているディーゼルエンジン1では、ターボチャージ
ャ2が備えられており、エアクリーナ3から導いた空気
4が吸気管5を介し前記ターボチャージャ2のコンプレ
ッサ2aへと送られ、該コンプレッサ2aで加圧された
空気4が更にインタクーラ6へと送られて冷却され、該
インタクーラ6から図示しないインテークマニホールド
へと空気4が導かれてディーゼルエンジン1の各シリン
ダに導入されるようにしてある。
FIG. 1 shows an embodiment of the present invention. In FIG. 1, reference numeral 1 denotes a diesel engine. In the diesel engine 1 shown here, a turbocharger 2 is provided, and an air cleaner 3 is provided. 4 is sent to a compressor 2a of the turbocharger 2 through an intake pipe 5, and the air 4 pressurized by the compressor 2a is further sent to an intercooler 6 to be cooled. The air 4 is guided to the intake manifold which is not used and introduced into each cylinder of the diesel engine 1.

【0018】また、このディーゼルエンジン1の各シリ
ンダには、図示しない燃料タンクからの液体燃料(軽
油)がディーゼルエンジン1の各シリンダ内に噴射され
て燃焼されるようにしてあり、ディーゼルエンジン1の
各シリンダから排出された排気ガス7がエキゾーストマ
ニホールド8を介し前記ターボチャージャ2のタービン
2bへと送られ、該タービン2bを駆動した排気ガス7
が排気管9を介し車外へ排出されるようにしてある。
In each cylinder of the diesel engine 1, liquid fuel (light oil) from a fuel tank (not shown) is injected into each cylinder of the diesel engine 1 and burned. Exhaust gas 7 discharged from each cylinder is sent to a turbine 2b of the turbocharger 2 via an exhaust manifold 8, and the exhaust gas 7 driving the turbine 2b
Is discharged outside the vehicle through the exhaust pipe 9.

【0019】そして、排気ガス7が流通する排気管9の
途中には、排気ガス7中の酸素濃度が高い時にNOxを
酸化して硝酸塩の状態で一時的に吸蔵し且つ排気ガス7
中の酸素濃度が低い時に後述する還元剤10(軽油)の
介在によりNOxを分解放出して還元浄化するNOx吸蔵
還元触媒11が装備されており、該NOx吸蔵還元触媒
11を迂回するように排気管9にバイパス流路12が付
設されている。
In the middle of the exhaust pipe 9 through which the exhaust gas 7 flows, when the oxygen concentration in the exhaust gas 7 is high, NOx is oxidized to temporarily store NOx in the state of nitrate, and the exhaust gas 7
A NOx storage-reduction catalyst 11 that decomposes and releases NOx by the interposition of a reducing agent 10 (light oil) to be described below when the oxygen concentration is low is provided, and the exhaust gas is bypassed so as to bypass the NOx storage-reduction catalyst 11. The pipe 9 is provided with a bypass channel 12.

【0020】ここで、排気管9に対するバイパス流路1
2の分岐箇所には、排気管9を流れる排気ガス7を適宜
にバイパス流路12側に切り替えて流し得るよう流路切
換弁13,14が夫々設けられている。
Here, the bypass passage 1 for the exhaust pipe 9 is provided.
At the two branch points, flow path switching valves 13 and 14 are provided so that the exhaust gas 7 flowing through the exhaust pipe 9 can be appropriately switched to the bypass flow path 12 and flow therethrough.

【0021】また、排気管9におけるNOx吸蔵還元触
媒11の入側には、噴射ノズル15が配設されており、
該噴射ノズル15と所定場所の還元剤タンク16(燃料
タンクと兼用することも可)との間が還元剤供給管17
により接続されていると共に、前記噴射ノズル15と所
定場所のエアタンク18との間が空気導入管19により
接続されており、前記還元剤供給管17の途中の送給ポ
ンプ20を駆動して還元剤タンク16内の還元剤10を
噴射ノズル15に導くことにより該噴射ノズル15から
NOx吸蔵還元触媒11の入側に向け還元剤10を噴霧
し得るようにしてある。また、還元剤10の量が少ない
と霧化しづらい為、霧化させるためのアシストとして、
前記空気導入管19の途中の開閉弁21を開けて少量の
加圧空気を噴射ノズル15に導くことも可能な構造とな
っている。
An injection nozzle 15 is provided on the exhaust pipe 9 at the inlet of the NOx storage reduction catalyst 11.
A reducing agent supply pipe 17 is provided between the injection nozzle 15 and a reducing agent tank 16 at a predetermined location (which can also be used as a fuel tank).
In addition, the injection nozzle 15 and an air tank 18 at a predetermined location are connected by an air introduction pipe 19, and a feed pump 20 in the middle of the reducing agent supply pipe 17 is driven to reduce the reducing agent. The reducing agent 10 in the tank 16 is guided to the injection nozzle 15 so that the reducing agent 10 can be sprayed from the injection nozzle 15 toward the inlet side of the NOx storage reduction catalyst 11. Also, if the amount of the reducing agent 10 is small, it is difficult to atomize, so as an assist for atomizing,
The opening / closing valve 21 in the middle of the air introduction pipe 19 is opened so that a small amount of pressurized air can be guided to the injection nozzle 15.

【0022】尚、図中22は排気管9の下流側に備えた
マフラを示す。
In the figure, reference numeral 22 denotes a muffler provided on the downstream side of the exhaust pipe 9.

【0023】而して、ディーゼルエンジン1の運転時
に、流路切換弁13を開け且つ流路切換弁14を閉じて
酸素濃度の高い排気ガス7をNOx吸蔵還元触媒11に
流すと、排気ガス7中のNOxが硝酸塩の状態で吸蔵さ
れ、これによりディーゼルエンジン1の希薄燃焼運転時
における良好なNOxの低減化が図られることになる。
When the exhaust gas 7 having a high oxygen concentration flows through the NOx storage reduction catalyst 11 by opening the flow path switching valve 13 and closing the flow path switching valve 14 during operation of the diesel engine 1, the exhaust gas 7 The stored NOx is stored in the form of nitrate, whereby good reduction of NOx during the lean burn operation of the diesel engine 1 is achieved.

【0024】そして、このようなNOxの吸蔵を約30
秒〜3分程度続けた後に、流路切換弁14を開け且つ流
路切換弁13を閉じて排気ガス7をバイパス流路12側
へ迂回させて流し、送給ポンプ20の駆動により還元剤
タンク16から還元剤10を導き、必要に応じ開閉弁2
1を開けて少量の加圧空気を霧化のアシストとしてエア
タンク18から導く等して噴射ノズル15からNOx吸
蔵還元触媒11の入側に還元剤10を噴霧する。
Then, such NOx occlusion is reduced by about 30
After continuing for about 2 to 3 minutes, the flow path switching valve 14 is opened, the flow path switching valve 13 is closed, and the exhaust gas 7 is bypassed to the bypass flow path 12 to flow therethrough. The reducing agent 10 is guided from 16 and, if necessary, the on-off valve 2
1, the reducing agent 10 is sprayed from the injection nozzle 15 to the inlet side of the NOx storage reduction catalyst 11 by guiding a small amount of pressurized air from the air tank 18 as assist for atomization.

【0025】このようにすれば、還元剤10の添加量に
対する相対的な空気過剰率が低下して還元剤10とNO
xの反応選択性が向上し、これによりNOx吸蔵還元触媒
11からNOxが積極的に分解放出されて該NOx吸蔵還
元触媒11の良好な再生が図られ、その放出したNOx
がNOx吸蔵還元触媒11上で前記還元剤10と反応し
て還元浄化されることになる。
By doing so, the relative excess air ratio with respect to the amount of the reducing agent 10 added decreases, and the reducing agent 10 and NO
The reaction selectivity of x is improved, so that NOx is actively decomposed and released from the NOx storage-reduction catalyst 11, whereby good regeneration of the NOx storage-reduction catalyst 11 is achieved, and the released NOx
Reacts with the reducing agent 10 on the NOx storage reduction catalyst 11 to be reduced and purified.

【0026】更に、約10〜30時間(高負荷運転で約
10〜15時間、中負荷運転で約20〜30時間)に一
回程度の割合で定期的に以下に詳述する如きNOx吸蔵
還元触媒11の脱硫処理を施すようにする。
Further, NOx storage reduction as described in detail below is performed periodically at a rate of about once every about 10 to 30 hours (about 10 to 15 hours for high load operation, about 20 to 30 hours for medium load operation). The desulfurization treatment of the catalyst 11 is performed.

【0027】即ち、流路切換弁13を開け且つ流路切換
弁14を閉じて排気ガス7をNOx吸蔵還元触媒11に
流しつつ還元剤10を前述と同様にしてNOx吸蔵還元
触媒11の入側に噴霧して添加し、これにより排気ガス
7が流通している酸素濃度の高い高温雰囲気下での還元
剤10の酸化反応による発熱でNOx吸蔵還元触媒11
を約650〜700℃に昇温させ、その直後に流路切換
弁14を開け且つ流路切換弁13を閉じて排気ガス7を
バイパス流路12側へ迂回させて流しながらNOx吸蔵
還元触媒11に再び還元剤10を添加する。
That is, the flow path switching valve 13 is opened, the flow path switching valve 14 is closed, and the exhaust gas 7 flows to the NOx storage reduction catalyst 11 while the reducing agent 10 is supplied to the inlet side of the NOx storage reduction catalyst 11 in the same manner as described above. To the NOx storage reduction catalyst 11 by heat generated by the oxidation reaction of the reducing agent 10 in a high-temperature atmosphere with a high oxygen concentration in which the exhaust gas 7 is flowing.
The temperature is raised to about 650 to 700 ° C., and immediately after that, the flow switching valve 14 is opened and the flow switching valve 13 is closed, and the NOx storage reduction catalyst 11 Is added again with the reducing agent 10.

【0028】このようにすれば、還元剤10の添加量に
対する相対的な空気過剰率が低下して理論空燃比より小
さな空燃比のリッチ雰囲気が実現されることになるの
で、NOx吸蔵還元触媒11からSO2を放出させるため
の条件がディーゼルエンジン1側の運転制御を行わずに
整うことになり、NOx吸蔵還元触媒11が効率良く脱
硫処理されて硫酸塩による被毒が解消されることにな
る。
In this manner, the relative excess ratio of air to the amount of the reducing agent 10 is reduced, and a rich atmosphere having an air-fuel ratio smaller than the stoichiometric air-fuel ratio is realized. conditions for releasing SO 2 becomes the ready without operation control of the diesel engine 1 side, so that the poisoning is eliminated by sulfate NOx occlusion reduction catalyst 11 is efficiently desulfurized from .

【0029】ここで、NOx吸蔵還元触媒11の脱硫処
理に関しては、図2に示す如く、前述した如き還元剤1
0の二段添加による脱硫処理を1サイクルとして約15
分間程度に亘り数サイクル繰り返すモードを予め設定し
ておき、NOx吸蔵還元触媒11における大半の硫酸塩
をSO2として放出させて被毒劣化を十分に回復させる
ようにすることが好ましい。
Here, as for the desulfurization treatment of the NOx storage reduction catalyst 11, as shown in FIG.
The desulfurization treatment by two-stage addition of 0 is about 15 cycles.
Preferably, a mode in which several cycles are repeated for about a minute is set in advance, and most of the sulfate in the NOx storage reduction catalyst 11 is released as SO 2 to sufficiently recover poisoning deterioration.

【0030】従って、本形態例によれば、ディーゼルエ
ンジンの排気ガスをNOx吸蔵還元触媒で浄化するにあ
たり、該NOx吸蔵還元触媒の硫酸塩による被毒をディ
ーゼルエンジン側の運転制御を行わずに解消することが
できるので、NOx吸蔵還元触媒を使用した排気浄化装
置のディーゼルエンジンへの適用を実現することができ
る。
Therefore, according to this embodiment, when purifying the exhaust gas of the diesel engine with the NOx storage reduction catalyst, the poisoning of the NOx storage reduction catalyst by the sulfate is eliminated without performing the operation control on the diesel engine side. Therefore, the application of the exhaust gas purification device using the NOx storage reduction catalyst to a diesel engine can be realized.

【0031】図3は本発明を実施する形態の別の例を示
すもので、この形態例においては、前述した図1におけ
るNOx吸蔵還元触媒11を並列に対で設け、該各NOx
吸蔵還元触媒11,11の夫々に対して適宜に排気ガス
7を振り替えて流し得るよう排気管9を二つの分岐流路
9A,9Bに分岐させて前記各NOx吸蔵還元触媒1
1,11に接続し且つその下流側で再び合流させてマフ
ラ22に導くように構成してあり、前記各分岐流路9
A,9Bの分岐箇所には、排気管9を流れる排気ガス7
を各分岐流路9A,9Bに対し交互に切り替えて流し得
るよう流路切換弁13,14が夫々設けられている。
FIG. 3 shows another embodiment of the present invention. In this embodiment, the NOx storage reduction catalysts 11 shown in FIG.
The exhaust pipe 9 is branched into two branch passages 9A and 9B so that the exhaust gas 7 can be appropriately switched and flown to each of the storage reduction catalysts 11 and 11 so that the respective NOx storage reduction catalysts 1 are separated.
1 and 11 and are joined again on the downstream side to lead to the muffler 22.
Exhaust gas 7 flowing through the exhaust pipe 9
Are respectively provided so as to be able to alternately flow through the branch flow paths 9A and 9B.

【0032】また、各NOx吸蔵還元触媒11,11の
双方の入側には、図1の場合と同様に、噴射ノズル15
が配設されており、該各噴射ノズル15,15の何れに
対しても、還元剤タンク16内の還元剤10を送給ポン
プ20,20の駆動により還元剤供給管17,17を介
して導き且つ必要に応じてエアタンク18の加圧空気を
開閉弁21,21の開放により空気導入管19,19を
介し少量導いて各NOx吸蔵還元触媒11,11の入側
に還元剤10を選択的に噴霧し得るようにしてある。
As shown in FIG. 1, an injection nozzle 15 is provided on both sides of each of the NOx storage reduction catalysts 11, 11.
The reducing agent 10 in the reducing agent tank 16 is supplied to each of the injection nozzles 15 and 15 via the reducing agent supply pipes 17 and 17 by driving the supply pumps 20 and 20. Guided and pressurized air in the air tank 18 is guided through the air introduction pipes 19 and 19 as needed to open the on-off valves 21 and 21 to selectively supply the reducing agent 10 to the inlet side of each NOx storage reduction catalyst 11. So that it can be sprayed.

【0033】而して、このようにNOx吸蔵還元触媒1
1を並列に対で設けた場合には、流路切換弁13を開け
且つ流路切換弁14を閉じて排気ガス7を分岐流路9A
に流し、該分岐流路9AのNOx吸蔵還元触媒11によ
り排気ガス7中のNOxを硝酸塩の状態で吸蔵させてい
る間に、排気ガス7の流量が制限されている分岐流路9
B側のNOx吸蔵還元触媒11を再生したり、脱硫処理
を施したりするといった具合に、常にNOx吸蔵還元触
媒11,11のうちの何れか一方を使用可能な状態とし
て連続的にNOxの低減化を図ることができるわけであ
るが、斯かる構成の排気浄化装置の場合にも、本発明の
運転方法を同様に適用できることは当然である。
Thus, the NOx storage reduction catalyst 1
1 are provided in parallel, the flow path switching valve 13 is opened and the flow path switching valve 14 is closed to exhaust gas 7 into the branch flow path 9A.
While the NOx in the exhaust gas 7 is stored in the state of nitrate by the NOx storage reduction catalyst 11 in the branch flow path 9A, the flow rate of the exhaust gas 7 is restricted.
When the NOx storage reduction catalyst 11 on the B side is regenerated or subjected to a desulfurization treatment, one of the NOx storage reduction catalysts 11 and 11 is always in a usable state to continuously reduce NOx. However, it goes without saying that the operation method of the present invention can be similarly applied to the exhaust gas purification apparatus having such a configuration.

【0034】尚、本発明の排気浄化装置の運転方法は、
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。
The operation method of the exhaust gas purifying apparatus of the present invention is as follows.
It is needless to say that the present invention is not limited to the above-described embodiment, and that various changes can be made without departing from the spirit of the present invention.

【0035】[0035]

【発明の効果】上記した本発明の排気浄化装置の運転方
法によれば、ディーゼルエンジンの排気ガスをNOx吸
蔵還元触媒で浄化するにあたり、該NOx吸蔵還元触媒
の硫酸塩による被毒をディーゼルエンジン側の運転制御
を行わずに解消することができるので、NOx吸蔵還元
触媒を使用した排気浄化装置のディーゼルエンジンへの
適用を実現することができるという優れた効果を奏し得
る。
According to the operation method of the exhaust gas purifying apparatus of the present invention, when the exhaust gas of the diesel engine is purified by the NOx storage reduction catalyst, the poisoning of the NOx storage reduction catalyst by the sulfate is performed on the diesel engine side. Therefore, it is possible to achieve an excellent effect that the application of the exhaust purification device using the NOx storage reduction catalyst to a diesel engine can be realized.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明を実施する形態の一例を示す概略図であ
る。
FIG. 1 is a schematic diagram showing an example of an embodiment for implementing the present invention.

【図2】脱硫処理のモードのタイムスケジュールを示す
図である。
FIG. 2 is a diagram showing a time schedule of a desulfurization processing mode.

【図3】本発明を実施する形態の別の例を示す概略図で
ある。
FIG. 3 is a schematic diagram showing another example of the embodiment for carrying out the present invention.

【符号の説明】[Explanation of symbols]

1 ディーゼルエンジン 7 排気ガス 9 排気管 10 還元剤 11 NOx吸蔵還元触媒 DESCRIPTION OF SYMBOLS 1 Diesel engine 7 Exhaust gas 9 Exhaust pipe 10 Reducing agent 11 NOx storage reduction catalyst

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F01N 3/36 F01N 3/36 B ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) F01N 3/36 F01N 3/36 B

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ディーゼルエンジンからの排気ガスが流
通する排気管の途中に、排気ガス中の酸素濃度が高い時
にNOxを酸化して硝酸塩の状態で一時的に吸蔵し且つ
排気ガス中の酸素濃度が低い時に還元剤の介在によりN
Oxを分解放出して還元浄化するNOx吸蔵還元触媒を装
備し、該NOx吸蔵還元触媒に対し還元剤を適宜に添加
し且つ前記NOx吸蔵還元触媒を適宜に迂回させて排気
ガスを流し得るように構成した排気浄化装置の運転方法
であって、通常はディーゼルエンジンの排気ガスをNO
x吸蔵還元触媒に流し、これにより排気ガス中のNOxを
NOx吸蔵還元触媒に吸蔵させてNOxの低減化を図る一
方、定期的に排気ガスをNOx吸蔵還元触媒を迂回させ
て流しながら該NOx吸蔵還元触媒に還元剤を添加し、
これによりNOx吸蔵還元触媒からNOxを積極的に分解
放出させて該NOx吸蔵還元触媒の再生を図り、更に
は、定期的にNOx吸蔵還元触媒に排気ガスを流しつつ
還元剤を添加してNOx吸蔵還元触媒を所定温度以上に
昇温させ且つその直後にNOx吸蔵還元触媒を迂回させ
て排気ガスを流しながらNOx吸蔵還元触媒に再び還元
剤を添加して脱硫処理を施すことを特徴とする排気浄化
装置の運転方法。
In the exhaust pipe through which exhaust gas from a diesel engine flows, when the oxygen concentration in the exhaust gas is high, NOx is oxidized and temporarily stored in the form of nitrate, and the oxygen concentration in the exhaust gas is reduced. When the pressure is low, N
A NOx storage reduction catalyst that decomposes and releases Ox to reduce and purify the exhaust gas is provided so that a reducing agent is appropriately added to the NOx storage reduction catalyst and the NOx storage reduction catalyst is appropriately bypassed to allow exhaust gas to flow. This is a method of operating the exhaust gas purification device thus configured.
While flowing NOx in the NOx storage reduction catalyst to thereby reduce NOx, NOx in the exhaust gas is reduced by the NOx storage reduction catalyst. Add a reducing agent to the reduction catalyst,
As a result, the NOx storage reduction catalyst is actively decomposed and released from the NOx storage reduction catalyst to regenerate the NOx storage reduction catalyst, and further, a reducing agent is added to the NOx storage reduction catalyst while periodically flowing exhaust gas thereto to store NOx. Exhaust purification characterized by raising the temperature of the reduction catalyst to a predetermined temperature or higher, and immediately thereafter adding a reducing agent to the NOx storage reduction catalyst again while flowing exhaust gas while bypassing the NOx storage reduction catalyst to perform desulfurization treatment. How to operate the device.
JP2000294052A 2000-09-27 2000-09-27 Operating method of exhaust gas purification device Expired - Fee Related JP3545691B2 (en)

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US8578703B2 (en) 2004-02-02 2013-11-12 Nissan Diesel Motor Co., Ltd. Exhaust emission purifying apparatus for internal combustion engine
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US8037676B2 (en) 2005-11-21 2011-10-18 Isuzu Motors Limited Regeneration control method for exhaust gas purification system, and exhaust gas purification system
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