JP2003328742A - Exhaust emission control device of internal-combustion engine - Google Patents

Exhaust emission control device of internal-combustion engine

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Publication number
JP2003328742A
JP2003328742A JP2002142581A JP2002142581A JP2003328742A JP 2003328742 A JP2003328742 A JP 2003328742A JP 2002142581 A JP2002142581 A JP 2002142581A JP 2002142581 A JP2002142581 A JP 2002142581A JP 2003328742 A JP2003328742 A JP 2003328742A
Authority
JP
Japan
Prior art keywords
exhaust gas
catalyst
fuel ratio
exhaust
air
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
JP2002142581A
Other languages
Japanese (ja)
Other versions
JP4224984B2 (en
Inventor
Minoru Masuda
稔 益田
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor Corp
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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP2002142581A priority Critical patent/JP4224984B2/en
Publication of JP2003328742A publication Critical patent/JP2003328742A/en
Application granted granted Critical
Publication of JP4224984B2 publication Critical patent/JP4224984B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide an exhaust emission control device for an internal-combustion engine capable of raising the temperature of a catalyst effectively and quickly. <P>SOLUTION: A first cylinder group 1a and a second cylinder group 1b are connected with a three-dimensional catalyst 12 through Y-pipes 3 and 4, and then connected with a NOX catalyst 11. The air-fuel ratio of the exhaust gas flowing through a branch part 3a of the Y-pipe 3 is held lean while the air-fuel ratio of the exhaust gas flowing through another branch part 3b of the Y-pipe 3 is held rich for raising the temperature of the NOX catalyst 11, and the mean air-fuel ratio of the whole exhaust gas flowing into the three-dimensional catalyst 12 at this time is made the theoretical air-fuel ratio or richer to a minor extent. At the divergent part 4c of the Y-pipe 4 revolving device 13 is installed to guide the exhaust gas so that it revolves approximately round the axis of the divergent part 4c of the Y-pipe 4, and the exhaust gases from the two branch parts 3a and 3b are mixed together by the revolving device 13. <P>COPYRIGHT: (C)2004,JPO

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】本発明は内燃機関の排気浄化
装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas purification device for an internal combustion engine.

【0002】[0002]

【従来の技術】複数の気筒を一対の気筒群に分割し、こ
れら気筒群に接続された一対の上流側排気通路が合流し
て形成される下流側排気通路内に、流入する排気ガスの
空燃比がリーンのときに流入する排気ガス中のNO
蓄え、流入する排気ガスの空燃比が低下したときに排気
ガス中に還元剤が含まれていると蓄えているNOを還
元して蓄えているNOの量が減少するNO触媒を配
置し、NO触媒の温度を上昇させるために、一方の気
筒群で燃焼される混合気の空燃比をリーンに保持しかつ
他方の気筒群で燃焼される混合気の空燃比をリッチに保
持すると共に、このときNO触媒内に流入する排気ガ
ス全体の平均空燃比が理論空燃比になるようにした内燃
機関の排気浄化装置が公知である(特開平8−6105
2号公報参照)。
2. Description of the Related Art A plurality of cylinders are divided into a pair of cylinder groups, and a pair of upstream side exhaust passages connected to these cylinder groups are joined to form a downstream side exhaust passage. When the fuel ratio is lean, NO X in the inflowing exhaust gas is stored, and when the air-fuel ratio of the inflowing exhaust gas is reduced, the stored NO X is reduced if the reducing agent is contained in the exhaust gas. A NO X catalyst that reduces the amount of NO X stored is arranged, and in order to raise the temperature of the NO X catalyst, the air-fuel ratio of the air-fuel mixture burned in one cylinder group is kept lean and the other cylinder is An exhaust gas purification device for an internal combustion engine is known in which the air-fuel ratio of the air-fuel mixture burned in the group is kept rich and the average air-fuel ratio of the entire exhaust gas flowing into the NO X catalyst at this time is set to the theoretical air-fuel ratio. (JP-A-8-6105)
No. 2).

【0003】この場合、一方の気筒群から排出される排
気ガス中には多量の酸素が含まれており、他方の気筒群
から排出される排気ガス中には多量の未燃HC,COが
含まれている。従って、これら酸素及び未燃HC,CO
がNO触媒に到りNO触媒内で反応すると、NO
触媒の温度が上昇せしめられる。
In this case, the exhaust gas discharged from one cylinder group contains a large amount of oxygen, and the exhaust gas discharged from the other cylinder group contains a large amount of unburned HC and CO. Has been. Therefore, these oxygen and unburned HC, CO
When There reacted in NO X catalyst Italian the NO X catalyst, NO X
The temperature of the catalyst is raised.

【0004】[0004]

【発明が解決しようとする課題】一方の気筒群から排出
された排気ガスと、他方の気筒群から排出された排気ガ
スとは共に下流側排気通路内に流入して合流する。しか
しながら、これらの排気ガスがNO触媒に到るまでに
良好に混合ないし攪拌されるとは限らず、むしろ酸素及
び未燃HC,COが偏在したままNO触媒内に流入す
る恐れがある。この場合には、NO触媒に供給される
未燃HC,COをNO触媒の温度上昇のために有効に
利用できなくなり、更に、NO触媒の温度を目標温度
まで上昇させるのに長時間を要することにもなる。上述
の公報はこの問題点について何ら示唆していない。
The exhaust gas discharged from one cylinder group and the exhaust gas discharged from the other cylinder group both flow into the downstream exhaust passage and join together. However, these exhaust gases are not always mixed or stirred well until they reach the NO X catalyst, and rather, oxygen and unburned HC and CO may flow into the NO X catalyst while being unevenly distributed. In this case, unburned HC to be supplied to the NO X catalyst, will not be able to effectively use the CO for the temperature rise of the NO X catalyst, further, a long time the temperature of the NO X catalyst to raise up to the target temperature Will also be required. The above mentioned publication does not suggest this problem at all.

【0005】そこで本発明の目的は、触媒の温度を効果
的にかつ速やかに上昇させることができる内燃機関の排
気浄化装置を提供することにある。
Therefore, an object of the present invention is to provide an exhaust gas purifying apparatus for an internal combustion engine which can effectively and quickly raise the temperature of the catalyst.

【0006】[0006]

【課題を解決するための手段】前記課題を解決するため
に1番目の発明によれば、複数の気筒を一対の気筒群に
分割し、これら気筒群に接続された一対の上流側排気通
路が合流して形成される下流側排気通路内に酸化能を有
する触媒を配置し、該触媒の温度を上昇させるために、
一方の上流側排気通路から下流側排気通路内に流出する
排気ガスの空燃比をリーンに保持しかつ他方の上流側排
気通路から下流側排気通路内に流出する排気ガスの空燃
比をリッチに保持すると共に、このとき下流側排気通路
内に流入する排気ガス全体の平均空燃比が理論空燃比又
はわずかばかりリッチになるようにした内燃機関の排気
浄化装置において、前記触媒上流の下流側排気通路内
に、一方の上流側排気通路からの排気ガスと他方の上流
側排気通路からの排気ガスとを混合する混合手段を配置
している。
According to the first aspect of the present invention, a plurality of cylinders are divided into a pair of cylinder groups, and a pair of upstream side exhaust passages connected to these cylinder groups are provided. In order to raise the temperature of the catalyst by arranging a catalyst having oxidizing ability in the downstream side exhaust passage formed by confluence,
The lean air-fuel ratio of the exhaust gas flowing from one upstream exhaust passage into the downstream exhaust passage and the rich air-fuel ratio of the exhaust gas flowing from the other upstream exhaust passage into the downstream exhaust passage In addition, at this time, in the exhaust gas purification device of the internal combustion engine, wherein the average air-fuel ratio of the entire exhaust gas flowing into the downstream side exhaust passage becomes a theoretical air-fuel ratio or slightly rich, in the downstream side exhaust passage upstream of the catalyst. The mixing means for mixing the exhaust gas from the one upstream exhaust passage and the exhaust gas from the other upstream exhaust passage is arranged in the.

【0007】また、2番目の発明によれば1番目の発明
において、前記触媒上流の下流側排気通路内に酸化能を
有する追加の触媒を配置し、該追加の触媒上流の下流側
排気通路内に前記混合手段を配置している。
According to a second aspect of the present invention, in the first aspect, an additional catalyst having an oxidizing ability is disposed in the downstream exhaust passage upstream of the catalyst, and the additional catalyst upstream of the downstream exhaust passage is provided. The mixing means is arranged in.

【0008】また、3番目の発明によれば2番目の発明
において、前記混合手段と前記触媒間の下流側排気通路
を互いに並列に延びる一対の分岐通路から形成し、これ
ら分岐通路内にそれぞれ前記追加の触媒を配置してい
る。
According to a third aspect of the present invention, in the second aspect, the downstream exhaust passage between the mixing means and the catalyst is formed of a pair of branch passages extending in parallel with each other. An additional catalyst is placed.

【0009】また、4番目の発明によれば1番目の発明
において、前記混合手段を、排気ガスが下流側排気通路
のほぼ中心軸線周りに旋回するように排気ガスを案内す
る旋回装置から形成している。
According to a fourth aspect of the present invention, in the first aspect, the mixing means is formed of a swirl device for guiding the exhaust gas so that the exhaust gas swirls around a substantially central axis of the downstream exhaust passage. ing.

【0010】また、5番目の発明によれば1番目の発明
において、前記内燃機関において燃焼がリーン空燃比の
もとで継続的に行われるようになっており、前記触媒
を、流入する排気ガスの空燃比がリーンのときに流入す
る排気ガス中のNOを蓄え、流入する排気ガスの空燃
比が低下したときに排気ガス中に還元剤が含まれている
と蓄えているNOを還元して蓄えているNOの量が
減少するNO触媒から形成している。
According to a fifth aspect of the present invention, in the first aspect of the present invention, the combustion is continuously performed in the internal combustion engine under a lean air-fuel ratio, and the exhaust gas flowing in the exhaust gas flowing through the catalyst is introduced. air-fuel ratio is stored the NO X in the exhaust gas flowing at the time of lean, reducing the NO X when the air-fuel ratio of the inflowing exhaust gas is stored that contains a reducing agent in the exhaust gas when the reduction in It is formed from a NO X catalyst that reduces the amount of NO X stored.

【0011】また、6番目の発明によれば2番目又は3
番目の発明において、前記追加の触媒を三元触媒から形
成している。
According to the sixth aspect, the second or third aspect
In the second invention, the additional catalyst is formed from a three-way catalyst.

【0012】なお、本明細書では排気通路の或る位置よ
りも上流の排気通路、燃焼室、及び吸気通路内に供給さ
れた空気と炭化水素HC及び一酸化炭素COとの比をそ
の位置における排気ガスの空燃比と称している。
In this specification, the ratio of the air supplied to the exhaust passage, the combustion chamber, and the intake passage upstream of a certain position of the exhaust passage to the hydrocarbons HC and carbon monoxide CO at that position. It is called the air-fuel ratio of exhaust gas.

【0013】[0013]

【発明の実施の形態】図1は本発明を火花点火式内燃機
関に適用した場合を示している。しかしながら本発明を
圧縮着火式内燃機関に適用することもできる。
FIG. 1 shows the case where the present invention is applied to a spark ignition type internal combustion engine. However, the present invention can also be applied to a compression ignition type internal combustion engine.

【0014】図1を参照すると、機関本体1は複数例え
ば六つの気筒を備えている。これら気筒は機関本体1の
中心軸線の一側において整列された例えば三つの気筒か
らなる第1の気筒群1aと、機関本体1の中心軸線の他
側において整列された例えば三つの気筒からなる第2の
気筒群1bとに分割されている。第1及び第2の気筒群
1a,1bはそれぞれ対応する排気マニホルド2a,2
bを介してY字管3のそれぞれ対応する枝部3a,3b
にそれぞれ接続され、Y字管3の合流部3cはY字管4
の合流部4cに接続される。Y字管4の一対の枝部4
a,4bにはそれぞれケーシング5の入口がそれぞれ接
続され、これらケーシング5の出口はY字管6及び排気
管7を介してケーシング8の入口に接続される。また、
ケーシング8の出口には排気管9が接続される。なお、
図1において符号10は各気筒の燃焼室内に配置された
電磁制御式燃料噴射弁を示している。
Referring to FIG. 1, the engine body 1 includes a plurality of, for example, six cylinders. These cylinders are, for example, a first cylinder group 1a composed of, for example, three cylinders arranged on one side of the central axis of the engine body 1, and a third cylinder composed of, for example, three cylinders arranged on the other side of the central axis of the engine body 1. It is divided into two cylinder groups 1b. The first and second cylinder groups 1a, 1b are respectively associated with corresponding exhaust manifolds 2a, 2
corresponding branch portions 3a, 3b of the Y-shaped tube 3 via b
And the confluence 3c of the Y-tube 3 is connected to the Y-tube 4 respectively.
Is connected to the merging portion 4c. A pair of branches 4 of the Y-tube 4
The inlets of the casing 5 are respectively connected to a and 4b, and the outlets of these casings 5 are connected to the inlet of the casing 8 via the Y-shaped pipe 6 and the exhaust pipe 7. Also,
An exhaust pipe 9 is connected to the outlet of the casing 8. In addition,
In FIG. 1, reference numeral 10 indicates an electromagnetically controlled fuel injection valve arranged in the combustion chamber of each cylinder.

【0015】ケーシング8内には酸化能を有する触媒1
1が収容され、本発明による実施例ではこの触媒11は
NO触媒から形成される。NO触媒11は例えばア
ルミナを担体とし、この担体上に例えばカリウムK、ナ
トリウムNa、リチウムLi、セシウムCsのようなア
ルカリ金属、バリウムBa、カルシウムCaのようなア
ルカリ土類、ランタンLa、イットリウムYのような希
土類から選ばれた少なくとも一つと、白金Pt、パラジ
ウムPd、ロジウムRh、イリジウムIrのような貴金
属とが担持されている。一方、ケーシング5内には酸化
能を有する追加の触媒12がそれぞれ収容される。本発
明による実施例では、追加の触媒12は三元触媒からそ
れぞれ形成される。
A catalyst 1 having an oxidizing ability is provided in the casing 8.
1 is accommodated, in the embodiment according to the present invention the catalyst 11 is formed from NO X catalyst. The NO X catalyst 11 uses, for example, alumina as a carrier, and potassium K, sodium Na, lithium Li, an alkali metal such as cesium Cs, an alkaline earth such as barium Ba, calcium Ca, lanthanum La, yttrium Y is used as a carrier on the carrier. At least one selected from the rare earths and a noble metal such as platinum Pt, palladium Pd, rhodium Rh, and iridium Ir are supported. On the other hand, the additional catalyst 12 having an oxidizing ability is housed in the casing 5. In the embodiment according to the invention, the additional catalysts 12 are each formed from a three-way catalyst.

【0016】更に図1を参照すると、Y字管3の枝部3
a,3bが合流してからY字管4の枝部4a,4bが分
岐するまでの、例えばY字管4の合流部4c内には旋回
装置13が配置される。この旋回装置13は図2に示さ
れるように、Y字管4の内壁面上に固定される外輪13
aと、外輪13aのほぼ中央に配置される内輪13b
と、周方向に互いに離間しつつ外輪13a及び内輪13
bにより支持される複数の羽根13cとを具備する。図
2においてハッチングが施された部分が羽根13cを示
している。
Still referring to FIG. 1, the branch 3 of the Y-tube 3
The swirl device 13 is arranged, for example, in the joining portion 4c of the Y-shaped pipe 4 from the joining of the a and 3b to the branching of the branch portions 4a and 4b of the Y-shaped pipe 4. As shown in FIG. 2, the turning device 13 includes an outer ring 13 fixed on the inner wall surface of the Y-shaped tube 4.
a, and an inner ring 13b arranged approximately at the center of the outer ring 13a
And the outer ring 13a and the inner ring 13 while being separated from each other in the circumferential direction.
a plurality of blades 13c supported by b. In FIG. 2, the hatched portion indicates the blade 13c.

【0017】これら羽根13cはY字管4の合流部4c
の中心軸線に沿って螺旋状に延びており、従って排気ガ
スはこの旋回装置13によって、Y字管4の合流部4c
のほぼ中心軸線周りに旋回するように案内される。な
お、本発明による実施例ではこれら羽根13cは回転で
きないが、排気ガスが旋回する限り、羽根13cを回転
可能に支持することもできる。
These blades 13c are the merging portion 4c of the Y-shaped tube 4.
Since the exhaust gas is spirally extended along the central axis of the, the swirling device 13 causes the exhaust gas to join the joining portion 4c of the Y-shaped pipe 4.
Is guided to rotate about the central axis of the. Although the blades 13c cannot rotate in the embodiment according to the present invention, the blades 13c can be rotatably supported as long as the exhaust gas swirls.

【0018】一方、第1及び第2の気筒群1a,1bは
それぞれ対応するサージタンク(図示しない)を介して
共通の吸気ダクト(図示しない)に接続されている。
On the other hand, the first and second cylinder groups 1a and 1b are connected to a common intake duct (not shown) via corresponding surge tanks (not shown).

【0019】電子制御ユニット40はデジタルコンピュ
ータからなり、双方向性バス41によって互いに接続さ
れたROM(リードオンリメモリ)42、RAM(ラン
ダムアクセスメモリ)43、CPU(マイクロプロセッ
サ)44、入力ポート45及び出力ポート46を具備す
る。排気管7にはNO触媒11内に流入する排気ガス
の平均空燃比を検出するための空燃比センサ49rが取
り付けられ、排気管9にはNO触媒11から流出した
排気ガスの温度を検出するための温度センサ49tが取
り付けられる。この排気ガスの温度はNO触媒11の
温度を表している。これらセンサ49r,49tの出力
電圧はそれぞれ対応するAD変換器47を介して入力ポ
ート45に入力される。また、アクセルペダル50には
アクセルペダル50の踏み込み量に比例した出力電圧を
発生する負荷センサ51が接続され、負荷センサ51の
出力電圧は対応するAD変換器47を介して入力ポート
45に入力される。更に入力ポート45にはクランクシ
ャフトが例えば30°回転する毎に出力パルスを発生す
るクランク角センサ52が接続される。一方、出力ポー
ト46は対応する駆動回路48を介して燃料噴射弁10
にそれぞれ接続される。
The electronic control unit 40 comprises a digital computer, and a ROM (Read Only Memory) 42, a RAM (Random Access Memory) 43, a CPU (Microprocessor) 44, an input port 45, and an input port 45, which are connected to each other by a bidirectional bus 41. The output port 46 is provided. An air-fuel ratio sensor 49r for detecting the average air-fuel ratio of the exhaust gas flowing into the NO X catalyst 11 is attached to the exhaust pipe 7, and the exhaust pipe 9 detects the temperature of the exhaust gas flowing out from the NO X catalyst 11. A temperature sensor 49t for mounting is attached. The temperature of this exhaust gas represents the temperature of the NO X catalyst 11. The output voltages of these sensors 49r and 49t are input to the input port 45 via the corresponding AD converters 47, respectively. A load sensor 51 that generates an output voltage proportional to the amount of depression of the accelerator pedal 50 is connected to the accelerator pedal 50, and the output voltage of the load sensor 51 is input to the input port 45 via the corresponding AD converter 47. It Further, the input port 45 is connected to a crank angle sensor 52 that generates an output pulse each time the crankshaft rotates, for example, 30 °. On the other hand, the output port 46 is connected to the fuel injection valve 10 via the corresponding drive circuit 48.
Respectively connected to.

【0020】NO触媒11は流入する排気ガスの平均
空燃比がリーンのときにはNOを蓄え、流入する排気
ガスの空燃比が低下したときに排気ガス中に還元剤が含
まれていると蓄えているNOを還元して蓄えているN
の量を減少させる蓄積還元作用を行う。
The NO X catalyst 11 stores NO X when the average air-fuel ratio of the inflowing exhaust gas is lean, and stores that the reducing agent is contained in the exhaust gas when the air-fuel ratio of the inflowing exhaust gas decreases. N that stores and stores NO X
Reducing the amount of O X to accumulate reducing action.

【0021】NO触媒の蓄積還元作用の詳細なメカニ
ズムについては完全には明らかにされていない。しかし
ながら、現在考えられているメカニズムを、担体上に白
金Pt及びバリウムBaを担持させた場合を例にとって
簡単に説明すると次のようになる。
The detailed mechanism of the NO X catalyst storage-reduction effect has not been completely clarified. However, the mechanism currently considered will be briefly described as follows, taking a case where platinum Pt and barium Ba are supported on a carrier as an example.

【0022】即ち、NO触媒に流入する排気ガスの空
燃比が理論空燃比よりもかなりリーンになると流入する
排気ガス中の酸素濃度が大巾に増大し、酸素OがO
又はO2−の形で白金Ptの表面に付着する。一方、
流入する排気ガス中のNOは白金Ptの表面上でO
又はO2−と反応し、NOとなる(NO+O→NO
)。次いで生成されたNOの一部は白金Pt上でさ
らに酸化されつつNO 触媒内に吸収されて酸化バリウ
ムBaOと結合しながら、硝酸イオンNO の形でN
触媒内に拡散する。このようにしてNOがNO
触媒内に蓄えられる。
That is, NOXEmpty exhaust gas flowing into the catalyst
Inflow when the fuel ratio becomes much leaner than the theoretical air-fuel ratio
The oxygen concentration in the exhaust gas greatly increases, and oxygen OTwoIs OTwo
Or O2-It adheres to the surface of platinum Pt in the form of. on the other hand,
NO in the inflowing exhaust gas is O on the surface of platinum Pt.Two
Or O2-Reacts with NOTwo(NO + OTwo→ NO
Two). NO generated nextTwoIs part of platinum on Pt
NO while being oxidized XAbsorbed inside the catalyst and oxidized
Nitrate ion NO while binding with BaOThree In the form of N
OXDiffuses in the catalyst. NO in this wayXIs NOX
It is stored in the catalyst.

【0023】これに対し、NO触媒に流入する排気ガ
スの空燃比がリッチ又は理論空燃比になると、排気ガス
中の酸素濃度が低下してNOの生成量が低下し、反応
が逆方向(NO →NO)に進み、斯くしてNO
媒内の硝酸イオンNO がNOの形でNO触媒から
放出される。この放出されたNOは排気ガス中に還元
剤即ちHC,COが含まれているとこれらHC,COと
反応して還元せしめられる。このようにして白金Ptの
表面上にNOが存在しなくなるとNO触媒から次か
ら次へとNOが放出されて還元され、NO触媒内に
蓄えられているNOの量が次第に減少する。
On the other hand, when the air-fuel ratio of the exhaust gas flowing into the NO X catalyst becomes rich or becomes the stoichiometric air-fuel ratio, the oxygen concentration in the exhaust gas lowers, the amount of NO 2 produced decreases, and the reaction proceeds in the opposite direction. Proceeding to (NO 3 → NO), the nitrate ions NO 3 in the NO X catalyst are thus released from the NO X catalyst in the form of NO. When the exhaust gas contains reducing agents, that is, HC and CO, the released NO X reacts with these HC and CO and is reduced. Thus NO X with the NO X is not present on the surface of the platinum Pt from NO X catalyst to the next from the next is reduced is released, the amount of the NO X that is stored in the NO X catalyst gradually Decrease.

【0024】なお、硝酸塩を形成することなくNO
蓄え、NOを放出することなくNOを還元すること
も可能である。
[0024] Incidentally, accumulated the NO X without forming a nitrate, can be reduced without any NO X to release NO X.

【0025】図1に示される内燃機関はリーン空燃比の
もとでの燃焼が継続して行われており、従ってNO
媒11内に流入する排気ガスの空燃比はリーンに維持さ
れている。その結果、排気ガス中のNOはNO触媒
11内に蓄えられる。
The internal combustion engine shown in FIG. 1 continues to perform combustion under a lean air-fuel ratio, so that the air-fuel ratio of the exhaust gas flowing into the NO X catalyst 11 is maintained lean. . As a result, NO X in the exhaust gas is stored in the NO X catalyst 11.

【0026】時間の経過と共にNO触媒11内の蓄積
NO量は次第に増大する。そこで本発明による実施例
では、例えばNO触媒11内の蓄積NO量が許容量
を越えたときには、NO触媒11内に流入する排気ガ
スの空燃比を一時的にリッチに切り替えるようにしてい
る。このようにすると、NO触媒11内の蓄積NO
量が減少し、このときNO触媒11からNOが流出
しない。
NO over timeXAccumulation in catalyst 11
NOXThe quantity increases gradually. Therefore, an embodiment according to the present invention
Then, for example, NOXAccumulated NO in catalyst 11XAmount is acceptable
NO is exceededXExhaust gas flowing into the catalyst 11
The air-fuel ratio of the engine is temporarily switched to rich.
It If this is done, NOXAccumulated NO in catalyst 11 X
The amount decreases, and at this time NOXNO from catalyst 11XLeaked
do not do.

【0027】ところが、排気ガス中にはイオウ分がSO
の形で含まれており、NO触媒11内にはNO
かりでなくSOも蓄えられる。このSOのNO
媒11内への蓄積メカニズムはNOの蓄積メカニズム
と同じであると考えられる。即ち、担体上に白金Pt及
びバリウムBaを担持させた場合を例にとって簡単に説
明すると、NO触媒11に流入する排気ガスの空燃比
がリーンのときには上述したように酸素OがO
はO2−の形で白金Ptの表面に付着しており、流入す
る排気ガス中のSOは白金Ptの表面上でO 又は
2−と反応し、SOとなる。次いで生成されたSO
は白金Pt上でさらに酸化されつつNO触媒11内
に吸収されて酸化バリウムBaOと結合しながら、硫酸
イオンSO の形でNO触媒11内に拡散する。こ
の硫酸イオンSO は次いでバリウムイオンBa
結合して硫酸塩BaSOを生成する。
However, the sulfur content in the exhaust gas is SO.
Included in the form of X, it is in the NO X catalyst 11 SO X also stored not only NO X. The mechanism of accumulation of SO X in the NO X catalyst 11 is considered to be the same as the mechanism of NO X accumulation. That is, the case where platinum Pt and barium Ba are carried on the carrier will be briefly described as an example. When the air-fuel ratio of the exhaust gas flowing into the NO X catalyst 11 is lean, as described above, the oxygen O 2 becomes O 2 −. Alternatively, it is attached to the surface of platinum Pt in the form of O 2− , and SO 2 in the inflowing exhaust gas reacts with O 2 or O 2− on the surface of platinum Pt to become SO 3 . SO generated next
3 is further oxidized on platinum Pt, absorbed in the NO X catalyst 11 and combined with barium oxide BaO, and diffuses in the NO X catalyst 11 in the form of sulfate ion SO 4 . The sulfate ion SO 4 then combines with the barium ion Ba + to produce the sulfate salt BaSO 4 .

【0028】この硫酸塩BaSOは分解しにくく、N
触媒11内に流入する排気ガスの空燃比をただ単に
リッチにしてもNO触媒11内の硫酸塩BaSO
量は減少しない。このため、時間が経過するにつれてN
触媒11内の硫酸塩BaSOの量が増大し、その
結果NO触媒11が蓄えうるNOの量が減少するこ
とになる。
This sulfate BaSO 4 is difficult to decompose and
Even if the air-fuel ratio of the exhaust gas flowing into the O X catalyst 11 is simply made rich, the amount of sulfate BaSO 4 in the NO X catalyst 11 does not decrease. Therefore, as time passes, N
O X amount of sulfate BaSO 4 catalyst 11 is increased, the amount of result NO X catalyst 11 can stored NO X is decreased.

【0029】しかしながら、NO触媒11の温度を例
えば550℃以上に維持しつつNO 触媒11に流入す
る排気ガスの空燃比を理論空燃比又はわずかばかりリッ
チにすると、NO触媒11内の硫酸塩BaSOが分
解してSOの形でNO触媒11から放出される。こ
の放出されたSOは排気ガス中に還元剤即ちHC,C
Oが含まれているとこれらHC,COと反応してSO
に還元せしめられる。このようにしてNO触媒11内
に蓄えられているSOの量が次第に減少し、このとき
NO触媒11からSOがSOの形で流出すること
がない。
However, NOXExample of temperature of catalyst 11
For example, NO while maintaining above 550 ℃ XFlow into catalyst 11
The exhaust gas air-fuel ratio
If you go to Chi, NOXSulfate BaSO in the catalyst 11FourMinutes
Understand SOThreeIn the form of NOXIt is released from the catalyst 11. This
SO releasedThreeIs a reducing agent in the exhaust gas, that is, HC, C
When O is contained, it reacts with these HC and CO, and SOTwo
Be reduced to. NO in this wayXInside the catalyst 11
SO stored inXThe amount of
NOXCatalyst 11 to SOXIs SOThreeSpill in the form of
There is no.

【0030】そこで本発明による実施例では、例えばN
触媒11内の蓄積SO量が許容量を越えたときに
は、NO触媒11内の蓄積SO量を減少させるため
に、NO触媒11の温度を550℃まで上昇し次いで
550℃以上に維持しながら、NO触媒11内に流入
する排気ガスの平均空燃比を理論空燃比又はわずかばか
りリッチに保持するようにしている。
Therefore, in the embodiment according to the present invention, for example, N
When storing SO X amount in the O X catalyst 11 exceeds the allowable amount, to reduce the accumulation SO X amount in the NO X catalyst 11, elevated and then 550 ° C. or higher temperature of the NO X catalyst 11 to 550 ° C. While maintaining the above, the average air-fuel ratio of the exhaust gas flowing into the NO X catalyst 11 is maintained at the stoichiometric air-fuel ratio or slightly rich.

【0031】具体的には、三元触媒12内に流入する排
気ガス全体の平均空燃比を理論空燃比又はわずかばかり
リッチになるようにしつつ、Y字管3の枝部3a内を流
通する排気ガスの空燃比をリーンに保持し、Y字管3の
枝部3b内を流通する排気ガスの空燃比が一時的にリッ
チに切り替えられる。その結果、比較的多量の酸素を含
む排気ガスと、比較的多量のHC,COを含む排気ガス
とが形成される。
Specifically, the exhaust gas flowing in the branch portion 3a of the Y-tube 3 is made while the average air-fuel ratio of the entire exhaust gas flowing into the three-way catalyst 12 is made to be the theoretical air-fuel ratio or slightly rich. The air-fuel ratio of the gas is kept lean, and the air-fuel ratio of the exhaust gas flowing in the branch portion 3b of the Y-shaped pipe 3 is temporarily switched to rich. As a result, an exhaust gas containing a relatively large amount of oxygen and an exhaust gas containing a relatively large amount of HC and CO are formed.

【0032】これら排気ガスはY字管3の合流部3c内
及びY字管4の合流部4c内で互いに合流した後に三元
触媒12内に流入し、その結果三元触媒12内において
排気ガス中に含まれる多量のHC,COが多量の酸素の
存在下で燃焼する。このため、三元触媒12から流出す
る排気ガスの温度が上昇され、この高温の排気ガスが次
いでNO触媒11内に流入することによりNO触媒
11の温度が上昇される。
These exhaust gases flow into the three-way catalyst 12 after merging with each other in the merging portion 3c of the Y-tube 3 and the merging portion 4c of the Y-tube 4, and as a result, the exhaust gas in the three-way catalyst 12 is exhausted. A large amount of HC and CO contained therein burns in the presence of a large amount of oxygen. Therefore, the temperature increase of the exhaust gas flowing out from the three-way catalyst 12, the temperature of the NO X catalyst 11 is raised by flowing into the NO X catalyst 11 is then exhaust gas at this high temperature.

【0033】この場合、排気ガスは三元触媒12内に流
入する前に旋回装置13によって旋回されており、その
結果枝部3aからの酸素と枝部3bからのHC,COと
が良好に攪拌され混合されている。従って、三元触媒1
2に供給されたHC,COが三元触媒12内で燃焼しや
すくなっており、即ちNO触媒11の温度を上昇させ
るために有効に利用されることになる。また、NO
媒11の温度を目標温度まで上昇させるために必要な時
間を短縮でき、更に、三元触媒12から流出するHC,
COの量を低減することができる。
In this case, the exhaust gas is swirled by the swirl device 13 before flowing into the three-way catalyst 12, so that the oxygen from the branch portion 3a and the HC and CO from the branch portion 3b are well stirred. And mixed. Therefore, the three-way catalyst 1
The HC and CO supplied to 2 are easily combusted in the three-way catalyst 12, that is, they are effectively used to raise the temperature of the NO X catalyst 11. Further, the time required to raise the temperature of the NO X catalyst 11 to the target temperature can be shortened, and further, the HC flowing out from the three-way catalyst 12
The amount of CO can be reduced.

【0034】なお、Y字管3の枝部3b内を流通する排
気ガスの空燃比をリッチに切り替えるには様々な方法が
ある。即ち、例えば第2の気筒群1bで燃焼される混合
気の空燃比をリッチに切り替える方法や、或いは、第2
の気筒群1bで燃焼される混合気の空燃比をリーンに保
持しながら、排気マニホルド2b又は枝部3b内に追加
の燃料を供給したり、爆発工程又は排気行程において第
2の気筒群1bの燃焼室内に燃料噴射弁10から追加の
燃料を供給する方法がある。
There are various methods for switching the air-fuel ratio of the exhaust gas flowing in the branch portion 3b of the Y-shaped pipe 3 to rich. That is, for example, a method of switching the air-fuel ratio of the air-fuel mixture burned in the second cylinder group 1b to rich, or the second method
While maintaining the air-fuel ratio of the air-fuel mixture combusted in the cylinder group 1b of lean in the lean, the additional fuel is supplied into the exhaust manifold 2b or the branch portion 3b, or the second cylinder group 1b of the second cylinder group 1b in the explosion process or the exhaust stroke. There is a method of supplying additional fuel from the fuel injection valve 10 into the combustion chamber.

【0035】図3は図1に示される実施例におけるY字
管3の枝部3a,3bの出口と、Y字管4の枝部4a,
4bの入口とを概略的に示しており、この例ではY字管
3の枝部3a,3bの出口中心を結ぶ直線L3と、Y字
管4の枝部4a,4bの出口中心を結ぶ直線L4とが互
いにほぼ平行になっている。なお、図3においてCCは
Y字管3の合流部3c及びY字管4の合流部4cにより
形成される合流室を示している。
FIG. 3 shows the outlets of the branch portions 3a and 3b of the Y-shaped tube 3 and the branch portions 4a and 4a of the Y-shaped tube 4 in the embodiment shown in FIG.
4b schematically shows an inlet of 4b, and in this example, a straight line L3 connecting the outlet centers of the branch portions 3a and 3b of the Y-shaped tube 3 and a straight line connecting the outlet centers of the branch portions 4a and 4b of the Y-shaped tube 4. L4 and L4 are substantially parallel to each other. In FIG. 3, CC indicates a merging chamber formed by the merging portion 3c of the Y-shaped pipe 3 and the merging portion 4c of the Y-shaped pipe 4.

【0036】Y字管3の枝部3a,3b内をそれぞれ流
通した排気ガスは合流室CC内にそれぞれ流出して合流
し、次いでY字管4の枝部4a,4b内に流入する。こ
のことは結局のところ、Y字管3の枝部3aから流出し
た排気ガスがY字管4の枝部4a,4bに分配され、枝
部3bから流出した排気ガスが枝部4a,4bに分配さ
れることを意味している。
The exhaust gases flowing through the branch portions 3a and 3b of the Y-shaped tube 3 respectively flow into the confluence chamber CC and merge, and then flow into the branch portions 4a and 4b of the Y-shaped tube 4. After all, this means that the exhaust gas flowing out from the branch portion 3a of the Y-shaped pipe 3 is distributed to the branch portions 4a and 4b of the Y-shaped pipe 4, and the exhaust gas flowing out from the branch portion 3b is distributed to the branch portions 4a and 4b. It means being distributed.

【0037】この場合、合流室CCの容積は比較的小さ
く、ここでの排気ガスの混合は期待できない。従って、
旋回装置13が設けられていないとしたならば、Y字管
3の枝部3a,3bからそれぞれ流出した排気ガスは例
えば枝部3a,3bの形状などに応じて定まる方向に、
それらの慣性でもって進行することになる。このため、
Y字管3の例えば枝部3aから流出した排気ガスのうち
の大部分がY字管4の枝部4a内に流入し残りのわずか
な一部が枝部4b内に流入する場合もあれば、排気ガス
の大部分が枝部4b内に流入し残りのわずかな一部が枝
部4a内に流入する場合もある。枝部3bから流出した
排気ガスについても同様なことが言える。その結果、一
方の三元触媒12には過剰のHC,COが供給され、他
方の三元触媒12には過剰の酸素が供給されるというこ
とになる。
In this case, the volume of the merging chamber CC is relatively small, and mixing of the exhaust gas here cannot be expected. Therefore,
Assuming that the swirl device 13 is not provided, the exhaust gas flowing out from the branch portions 3a and 3b of the Y-shaped pipe 3 is directed in a direction determined according to the shape of the branch portions 3a and 3b, for example.
It will proceed with those inertias. For this reason,
In some cases, most of the exhaust gas flowing out from the branch portion 3a of the Y-shaped tube 3 flows into the branch portion 4a of the Y-shaped tube 4 and a slight remaining portion thereof flows into the branch portion 4b. In some cases, most of the exhaust gas may flow into the branch portion 4b and the remaining small amount may flow into the branch portion 4a. The same applies to the exhaust gas flowing out from the branch portion 3b. As a result, excess HC and CO are supplied to one three-way catalyst 12, and excess oxygen is supplied to the other three-way catalyst 12.

【0038】そこで本発明による実施例では、排気ガス
を旋回させて混合するための旋回装置13を合流室CC
内に配置している。その結果、Y字管3の枝部3a,3
bから流出した排気ガスが十分に混合された後に、Y字
管4の枝部4a,4b内に流入する。従って、この場合
には、Y字管3の枝部3aから流出した排気ガスがY字
管4の枝部4a,4b内にほぼ均等に流入し、Y字管3
の枝部3bから流出した排気ガスがY字管4の枝部4
a,4b内にほぼ均等に流入しているということにな
る。このため、各三元触媒12に供給されるHC,CO
及び酸素に過不足が生じない。
Therefore, in the embodiment according to the present invention, the swirl device 13 for swirling and mixing the exhaust gas is provided in the confluence chamber CC.
It is placed inside. As a result, the branch portions 3a, 3 of the Y-shaped tube 3
After the exhaust gas flowing out from b is sufficiently mixed, it flows into the branch portions 4a and 4b of the Y-shaped pipe 4. Therefore, in this case, the exhaust gas flowing out from the branch portion 3a of the Y-shaped pipe 3 flows into the branch portions 4a and 4b of the Y-shaped pipe 4 substantially evenly, and the Y-shaped pipe 3
The exhaust gas flowing out from the branch portion 3b of the
This means that they are almost evenly flowing into a and 4b. Therefore, HC, CO supplied to each three-way catalyst 12
And there is no excess or deficiency in oxygen.

【0039】図4はY字管3の枝部3a,3bの出口中
心を結ぶ直線L3と、Y字管4の枝部4a,4bの出口
中心を結ぶ直線L4とが互いにほぼ垂直になっている場
合を示しており、この場合にも本発明を適用することが
できる。この場合に旋回装置13が設けられないとした
ならば、各三元触媒12の一部分に過剰のHC,COが
局所的に供給され、別の部分に過剰の酸素が局所的に供
給される恐れがある。この場合に旋回装置13を設けれ
ば、このような不具合を解決することができ、即ち旋回
装置13を設けることによってHC,CO及び酸素を各
三元触媒12全体に供給できるということになる。言い
換えると、三元触媒12全体を有効に利用できる。
In FIG. 4, a straight line L3 connecting the outlet centers of the branch portions 3a and 3b of the Y-shaped tube 3 and a straight line L4 connecting the outlet centers of the branch portions 4a and 4b of the Y-shaped tube 4 are substantially perpendicular to each other. The present invention can be applied to this case as well. In this case, if the swirl device 13 is not provided, excess HC and CO may be locally supplied to a part of each three-way catalyst 12, and excess oxygen may be locally supplied to another part. There is. In this case, if the swirl device 13 is provided, such a problem can be solved, that is, by providing the swirl device 13, HC, CO, and oxygen can be supplied to the entire three-way catalyst 12. In other words, the entire three-way catalyst 12 can be effectively used.

【0040】これまで述べてきた実施例では、旋回装置
13とNO触媒11間の排気通路を互いに並列に延び
る一対の分岐通路から形成し、これら分岐通路内にそれ
ぞれ三元触媒12を配置している。このようにすると各
三元触媒12の容量を小さくすることができ、従って機
関背圧が上昇するのを抑制できる。しかしながら、旋回
装置13とNO触媒11間の排気通路を単一の排気通
路から形成し、この単一の排気通路内に単一の三元触媒
を配置した場合にも本発明を適用することができる。或
いは、旋回装置13とNO触媒11間に三元触媒を配
置しない場合にも本発明を適用することができる。この
場合には、枝部3aからの酸素と枝部3bからのHC,
COとがNO触媒11内において互いに反応すること
になる。
In the above-described embodiments, the exhaust passage between the swirl device 13 and the NO X catalyst 11 is formed by a pair of branch passages extending in parallel with each other, and the three-way catalyst 12 is arranged in each of the branch passages. ing. In this way, the capacity of each three-way catalyst 12 can be reduced, and therefore, the back pressure of the engine can be prevented from increasing. However, the present invention can be applied to the case where the exhaust passage between the swirl device 13 and the NO X catalyst 11 is formed of a single exhaust passage, and the single three-way catalyst is arranged in the single exhaust passage. You can Alternatively, the present invention can be applied to the case where the three-way catalyst is not arranged between the swirl device 13 and the NO X catalyst 11. In this case, oxygen from the branch portion 3a and HC from the branch portion 3b,
CO and CO will react with each other in the NO X catalyst 11.

【0041】[0041]

【発明の効果】触媒の温度を効果的にかつ速やかに上昇
させることができる。
The temperature of the catalyst can be raised effectively and promptly.

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

【図1】内燃機関の全体図である。FIG. 1 is an overall view of an internal combustion engine.

【図2】旋回装置の正面図である。FIG. 2 is a front view of a turning device.

【図3】Y字管3,4の出口及び入口を概略的に示す図
である。
FIG. 3 is a diagram schematically showing an outlet and an inlet of Y-shaped tubes 3 and 4.

【図4】別の実施例におけるY字管3,4の出口及び入
口を概略的に示す図である。
FIG. 4 is a diagram schematically showing an outlet and an inlet of Y-shaped tubes 3 and 4 in another embodiment.

【符号の説明】[Explanation of symbols]

1a…第1の気筒群 1b…第2の気筒群 3,4…Y字管 11…NO触媒 12…三元触媒 13…旋回装置1a ... 1st cylinder group 1b ... 2nd cylinder group 3, 4 ... Y-tube 11 ... NO X catalyst 12 ... Three-way catalyst 13 ... Swirling device

───────────────────────────────────────────────────── 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 3/28 F01N 3/28 301H 301J ─────────────────────────────────────────────────── ─── Continued Front Page (51) Int.Cl. 7 Identification Code FI Theme Coat (Reference) F01N 3/28 F01N 3/28 301H 301J

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 複数の気筒を一対の気筒群に分割し、こ
れら気筒群に接続された一対の上流側排気通路が合流し
て形成される下流側排気通路内に酸化能を有する触媒を
配置し、該触媒の温度を上昇させるために、一方の上流
側排気通路から下流側排気通路内に流出する排気ガスの
空燃比をリーンに保持しかつ他方の上流側排気通路から
下流側排気通路内に流出する排気ガスの空燃比をリッチ
に保持すると共に、このとき下流側排気通路内に流入す
る排気ガス全体の平均空燃比が理論空燃比又はわずかば
かりリッチになるようにした内燃機関の排気浄化装置に
おいて、前記触媒上流の下流側排気通路内に、一方の上
流側排気通路からの排気ガスと他方の上流側排気通路か
らの排気ガスとを混合する混合手段を配置した内燃機関
の排気浄化装置。
1. A plurality of cylinders are divided into a pair of cylinder groups, and a catalyst having an oxidizing ability is arranged in a downstream side exhaust passage formed by joining a pair of upstream side exhaust passages connected to these cylinder groups. In order to raise the temperature of the catalyst, the lean air-fuel ratio of the exhaust gas flowing from one upstream exhaust passage into the downstream exhaust passage and the other upstream exhaust passage from the downstream exhaust passage Exhaust gas purification of the internal combustion engine, in which the air-fuel ratio of the exhaust gas flowing out to the exhaust gas is kept rich and the average air-fuel ratio of the entire exhaust gas flowing into the downstream exhaust passage at this time is made to be the theoretical air-fuel ratio or slightly rich In the device, an exhaust purification device for an internal combustion engine, wherein mixing means for mixing exhaust gas from one upstream exhaust passage and exhaust gas from the other upstream exhaust passage is arranged in the downstream exhaust passage upstream of the catalyst. .
【請求項2】 前記触媒上流の下流側排気通路内に酸化
能を有する追加の触媒を配置し、該追加の触媒上流の下
流側排気通路内に前記混合手段を配置した請求項1に記
載の内燃機関の排気浄化装置。
2. The catalyst according to claim 1, wherein an additional catalyst having an oxidizing ability is arranged in the downstream exhaust passage upstream of the catalyst, and the mixing means is arranged in the downstream exhaust passage upstream of the additional catalyst. Exhaust gas purification device for internal combustion engine.
【請求項3】 前記混合手段と前記触媒間の下流側排気
通路を互いに並列に延びる一対の分岐通路から形成し、
これら分岐通路内にそれぞれ前記追加の触媒を配置した
請求項2に記載の内燃機関の排気浄化装置。
3. A downstream exhaust passage between the mixing means and the catalyst is formed of a pair of branch passages extending in parallel with each other,
The exhaust gas purification device for an internal combustion engine according to claim 2, wherein the additional catalyst is arranged in each of the branch passages.
【請求項4】 前記混合手段を、排気ガスが下流側排気
通路のほぼ中心軸線周りに旋回するように排気ガスを案
内する旋回装置から形成した請求項1に記載の内燃機関
の排気浄化装置。
4. The exhaust gas purifying apparatus for an internal combustion engine according to claim 1, wherein the mixing means is formed of a swirl device that guides the exhaust gas so that the exhaust gas swirls around a substantially central axis of the downstream exhaust passage.
【請求項5】 前記内燃機関において燃焼がリーン空燃
比のもとで継続的に行われるようになっており、前記触
媒を、流入する排気ガスの空燃比がリーンのときに流入
する排気ガス中のNOを蓄え、流入する排気ガスの空
燃比が低下したときに排気ガス中に還元剤が含まれてい
ると蓄えているNOを還元して蓄えているNOの量
が減少するNO触媒から形成した請求項1に記載の内
燃機関の排気浄化装置。
5. In the internal combustion engine, combustion is continuously performed under a lean air-fuel ratio, and the catalyst is exhausted into the exhaust gas flowing into the exhaust gas when the air-fuel ratio of the exhaust gas flowing into the internal combustion engine is lean. NO x is stored, and when the air-fuel ratio of the inflowing exhaust gas decreases, if the reducing agent is contained in the exhaust gas, the stored NO x is reduced and the amount of stored NO x decreases. The exhaust emission control device for an internal combustion engine according to claim 1, which is formed of an X catalyst.
【請求項6】 前記追加の触媒を三元触媒から形成した
請求項2又は3に記載の内燃機関の排気浄化装置。
6. The exhaust emission control device for an internal combustion engine according to claim 2, wherein the additional catalyst is a three-way catalyst.
JP2002142581A 2002-05-17 2002-05-17 Exhaust gas purification device for internal combustion engine Expired - Lifetime JP4224984B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102933810A (en) * 2010-04-05 2013-02-13 卡特彼勒公司 Ring reductant mixer
WO2019194156A1 (en) * 2018-04-03 2019-10-10 いすゞ自動車株式会社 Exhaust pipe
JP2020172950A (en) * 2019-04-08 2020-10-22 メタウォーター株式会社 Piping unit
CN114577543A (en) * 2022-02-18 2022-06-03 中国环境科学研究院 System and method for detecting emission amount of particulate matters in tail gas

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102933810A (en) * 2010-04-05 2013-02-13 卡特彼勒公司 Ring reductant mixer
WO2019194156A1 (en) * 2018-04-03 2019-10-10 いすゞ自動車株式会社 Exhaust pipe
JP2019183666A (en) * 2018-04-03 2019-10-24 いすゞ自動車株式会社 Exhaust pipe
JP2020172950A (en) * 2019-04-08 2020-10-22 メタウォーター株式会社 Piping unit
CN114577543A (en) * 2022-02-18 2022-06-03 中国环境科学研究院 System and method for detecting emission amount of particulate matters in tail gas

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