JP2845052B2 - Exhaust gas purification device for internal combustion engine - Google Patents
Exhaust gas purification device for internal combustion engineInfo
- Publication number
- JP2845052B2 JP2845052B2 JP25830692A JP25830692A JP2845052B2 JP 2845052 B2 JP2845052 B2 JP 2845052B2 JP 25830692 A JP25830692 A JP 25830692A JP 25830692 A JP25830692 A JP 25830692A JP 2845052 B2 JP2845052 B2 JP 2845052B2
- Authority
- JP
- Japan
- Prior art keywords
- nox
- catalyst
- exhaust gas
- absorption
- release
- 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.)
- Expired - Lifetime
Links
Landscapes
- Exhaust Gas After Treatment (AREA)
Description
【0001】[0001]
【産業上の利用分野】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 purifying apparatus for an internal combustion engine.
【0002】[0002]
【従来の技術】本出願人は、排気ガスの空燃比がリーン
のときにはNOx を吸収し排気ガスの空燃比がストイキ
(理論空燃比)またはリッチのときには吸収したNOx
を放出すると共に放出されたNOx を還元するNOx 吸
放出触媒をディーゼル機関排気通路内に配置し、前記N
Ox 吸放出触媒からNOx を放出せしめて放出されたN
Ox を還元せしめるときにはNOx 吸放出触媒に還元剤
を供給して燃焼せしめるようにした内燃機関の排気浄化
装置を提案している。2. Description of the Related Art When the air-fuel ratio of exhaust gas is lean, the present applicant absorbs NOx, and the air-fuel ratio of exhaust gas becomes stoichiometric.
(Stoichiometric air-fuel ratio) or NOx absorbed when rich
A NOx absorption / release catalyst for releasing NOx and reducing the released NOx is disposed in a diesel engine exhaust passage;
NOx is released from the Ox absorption / release catalyst and the released N
There has been proposed an exhaust gas purifying apparatus for an internal combustion engine in which a reducing agent is supplied to a NOx absorption / release catalyst and burned when Ox is reduced.
【0003】[0003]
【発明が解決しようとする課題】ところがこの装置で
は、NOx 吸放出触媒に吸収されたNOx の放出還元時
に、排気ガス温度が低く触媒が活性温度に達していない
場合には、還元剤は触媒で燃焼しないために、排気ガス
中の酸素量が低下せず、この結果、NOx 吸放出触媒か
らNOx が放出されず、あるいはNOx が放出されても
十分に還元浄化されないという問題を生ずる。However, in this apparatus, when the exhaust gas temperature is low and the catalyst does not reach the activation temperature during the release and reduction of the NOx absorbed by the NOx absorption and release catalyst, the reducing agent is a catalyst. Since combustion does not occur, the amount of oxygen in the exhaust gas does not decrease. As a result, there is a problem that NOx is not released from the NOx absorption / release catalyst, or even if NOx is released, reduction and purification are not sufficiently performed.
【0004】[0004]
【課題を解決するための手段】上記問題点を解決するた
めの本発明によれば、排気ガスの空燃比がリーンのとき
にはNOx を吸収し排気ガスの空燃比がストイキまたは
リッチのときには吸収したNOx を放出すると共に放出
されたNOx を還元するNOx 吸放出触媒を機関排気通
路内に配置し、NOx 吸放出触媒からNOx を放出せし
めて還元せしめるときにはNOx 吸放出触媒に還元剤を
供給して燃焼せしめ、NOx 吸放出触媒での還元剤の燃
焼開始を促進するためにNOx 吸放出触媒の上流側端部
における白金の担持量をその他の部分における白金の担
持量よりも多くしている。According to the present invention for solving the above problems, NOx is absorbed when the air-fuel ratio of exhaust gas is lean, and is absorbed when the air-fuel ratio of exhaust gas is stoichiometric or rich. A NOx absorption / release catalyst for releasing NOx and reducing the released NOx is disposed in the engine exhaust passage. When NOx is released and reduced from the NOx absorption / release catalyst, a reducing agent is supplied to the NOx absorption / release catalyst to burn it. , The upstream end of the NOx adsorbing / releasing catalyst to promote the start of combustion of the reducing agent on the NOx adsorbing / releasing catalyst.
The amount of platinum carried in
You have more than your holdings .
【0005】[0005]
【作用】NOx 吸放出触媒からNOx を放出せしめて還
元せしめるときにはNOx 吸放出触媒に還元剤が供給さ
れて燃焼せしめられる。これによって、NOx 吸放出触
媒内の排気ガス中の酸素が消費されて酸素濃度が低下
し、このため、NOx 吸放出触媒からNOx が放出され
て還元剤によって還元される。When the NOx is released and reduced from the NOx absorption / release catalyst, a reducing agent is supplied to the NOx absorption / release catalyst and burned. As a result, oxygen in the exhaust gas in the NOx absorption / desorption catalyst is consumed and the oxygen concentration is reduced. Therefore, NOx is released from the NOx absorption / desorption catalyst and reduced by the reducing agent.
【0006】NOx 吸放出触媒の上流側端部における白
金の担持量をその他の部分における白金の担持量よりも
多くすることによってNOx 吸放出触媒での還元剤の燃
焼開始が促進されるために、排気ガスが低温であっても
還元剤が燃焼開始せしめられ、NOx を確実に還元せし
めることができる。[0006] The white at the upstream end of the NOx absorption / desorption catalyst
The amount of supported gold is higher than the amount of supported platinum in other parts.
By increasing the number, the start of combustion of the reducing agent in the NOx adsorbing / releasing catalyst is promoted. Therefore, even when the exhaust gas is at a low temperature, the reducing agent is started to burn, so that NOx can be surely reduced.
【0007】[0007]
【実施例】図1を参照すると、2はディーゼル機関本
体、4は吸気通路、6は排気通路を夫々示す。吸気通路
4内には吸気絞り弁8が設けられ、この吸気絞り弁8は
通常時は全開とされている。排気通路6の途中には、N
Ox 吸放出触媒10を内蔵したケーシング12が配置さ
れる。ケーシング12上流の排気通路6には還元剤とし
て燃料を供給するための燃料供給装置14が配置され
る。Referring to FIG. 1, reference numeral 2 denotes a diesel engine main body, 4 denotes an intake passage, and 6 denotes an exhaust passage. An intake throttle valve 8 is provided in the intake passage 4, and the intake throttle valve 8 is normally fully opened. In the middle of the exhaust passage 6, N
A casing 12 containing an Ox absorption / release catalyst 10 is provided. A fuel supply device 14 for supplying fuel as a reducing agent is disposed in the exhaust passage 6 upstream of the casing 12.
【0008】ケーシング12内に収容されているNOx
吸放出触媒10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L
i、セシウムCsのようなアルカリ金属、バリウムB
a、カルシウムCaのようなアルカリ土類、ランタンL
a、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のような貴金属とが担持されてい
る。NOx 吸放出触媒10は流入排気ガスの空燃比がリ
ーンのときにはNOx を吸収し、流入排気ガス中の酸素
濃度が低下すると吸収したNOx を放出するNOx の吸
放出作用を行う。[0008] NOx contained in the casing 12
The adsorption / desorption catalyst 10 uses, for example, alumina as a carrier, and, for example, potassium K, sodium Na, lithium L
i, alkali metal such as cesium Cs, barium B
a, alkaline earth such as calcium Ca, lanthanum L
a, at least one selected from rare earths such as yttrium Y and a noble metal such as platinum Pt are supported. The NOx absorption / release catalyst 10 absorbs NOx when the air-fuel ratio of the inflowing exhaust gas is lean, and performs an absorption / release operation of the NOx that releases the absorbed NOx when the oxygen concentration in the inflowing exhaust gas decreases.
【0009】上述のNOx 吸放出触媒10を機関排気通
路内に配置すればこのNOx 吸放出触媒10は実際にN
Ox の吸放出作用を行うがこの吸放出作用の詳細なメカ
ニズムについては明らかでない部分もある。しかしなが
らこの吸放出作用は図2に示すようなメカニズムで行わ
れているものと考えられる。次にこのメカニズムについ
て担体上に白金PtおよびバリウムBaを担持させた場
合を例にとって説明するが他の貴金属、アルカリ金属、
アルカリ土類、希土類を用いても同様なメカニズムとな
る。If the above-described NOx adsorbing / releasing catalyst 10 is disposed in the engine exhaust passage, the NOx adsorbing / releasing catalyst 10 actually
Ox is absorbed and released, but the detailed mechanism of the absorption and release is not clear in some parts. However, it is considered that this absorption / release action is performed by a mechanism as shown in FIG. Next, this mechanism will be described by taking as an example a case where platinum Pt and barium Ba are supported on a carrier, but other noble metals, alkali metals,
The same mechanism can be obtained by using alkaline earths and rare earths.
【0010】即ち、流入排気ガスがかなりリーンになる
と流入排気ガス中の酸素濃度が大巾に増大し、図2
(A)に示されるようにこれら酸素O2 がO2 - の形で
白金Ptの表面に付着する。一方、流入排気ガス中のN
Oは白金Ptの表面上でO2 - と反応し、NO2 となる
(2NO+O2 →2NO2 )。次いで生成されたNO2
の一部は白金Pt上で更に酸化されつつ吸放出触媒10
内に吸収されて酸化バリウムBaOと結合しながら、図
2(A)に示されるように硝酸イオンNO3 - の形で吸
放出触媒10内に拡散する。このようにしてNOx がN
Ox 吸放出触媒10内に吸収される。That is, when the inflowing exhaust gas becomes considerably lean, the oxygen concentration in the inflowing exhaust gas greatly increases.
As shown in (A), these oxygens O 2 adhere to the surface of platinum Pt in the form of O 2 − . On the other hand, N
O is O 2 on the surface of the platinum Pt - reacted with, and NO 2 (2NO + O 2 → 2NO 2). NO 2 generated
Is partially oxidized on platinum Pt while absorbing and releasing catalyst 10
Is absorbed while bonding with the barium oxide BaO within, nitrate ions NO 3 as shown in FIG. 2 (A) - diffuses into absorbing and releasing catalyst 10 in the form of. In this way, NOx becomes N
It is absorbed in the Ox absorption / desorption catalyst 10.
【0011】流入排気ガス中の酸素濃度が高い限り白金
Ptの表面でNO2 が生成され、吸放出触媒10のNO
x 吸収能力が飽和しない限りNO2 が吸放出触媒10内
に吸収されて硝酸イオンNO3 - が生成される。これに
対して流入排気ガス中の酸素濃度が低下してNO2 の生
成量が低下すると反応が逆方向(NO3 - →NO2 )に
進み、斯くして吸放出触媒10内の硝酸イオンNO3 -
がNO2 の形で吸収剤から放出される。即ち、流入排気
ガス中の酸素濃度が低下するとNOx 吸放出触媒10か
らNOx が放出されることになる。流入排気ガスのリー
ンの度合いが低くなれば流入排気ガス中の酸素濃度が低
下し、従って流入排気ガスのリーンの度合いを低くすれ
ばNOx 吸放出触媒10からNOx が放出されることに
なる。As long as the oxygen concentration in the inflowing exhaust gas is high, NO 2 is generated on the surface of the platinum Pt,
As long as the x absorption capacity is not saturated, NO 2 is absorbed in the absorption / desorption catalyst 10 to generate nitrate ions NO 3 − . On the other hand, when the oxygen concentration in the inflowing exhaust gas decreases and the amount of generated NO 2 decreases, the reaction proceeds in the opposite direction (NO 3 − → NO 2 ), and thus the nitrate ion NO 3 -
There are released from the absorbent in the form of NO 2. That is, when the oxygen concentration in the inflowing exhaust gas decreases, NOx is released from the NOx absorption / release catalyst 10. If the degree of leanness of the inflowing exhaust gas decreases, the concentration of oxygen in the inflowing exhaust gas decreases. Therefore, if the degree of leanness of the inflowing exhaust gas decreases, NOx is released from the NOx absorption / release catalyst 10.
【0012】一方、このとき流入排気ガスの空燃比をリ
ッチにすると、HC,COは白金Pt上の酸素O2 - と
反応して酸化せしめられる。また、流入排気ガスの空燃
比をリッチにすると流入排気ガス中の酸素濃度が極度に
低下するために吸放出触媒10からNO2 が放出され、
このNO2 は図2(B)に示されるように未燃HC,C
Oと反応して還元浄化せしめられる。このようにして白
金Ptの表面上にNO 2 が存在しなくなると吸放出触媒
10から次から次へとNO2 が放出される。従って流入
排気ガスの空燃比をリッチにすると短時間のうちにNO
x 吸放出触媒10からNOx が放出されて還元浄化され
ることになる。On the other hand, at this time, the air-fuel ratio of the inflowing exhaust gas is reset.
HC, CO is oxygen O on platinum Pt.Two -When
Reacts and oxidizes. Also, the air-fuel
When the ratio is made rich, the oxygen concentration in the inflow exhaust gas becomes extremely high.
NO from the adsorption / desorption catalyst 10TwoIs released,
This NOTwoAre the unburned HC and C as shown in FIG.
It reacts with O and is reduced and purified. White in this way
NO on the surface of gold Pt TwoIs no longer present
NO from 10 to next from 10TwoIs released. Therefore inflow
If the air-fuel ratio of the exhaust gas is made rich, NO
x NOx is released from the x absorption / desorption catalyst 10 and reduced and purified.
Will be.
【0013】このように流入排気ガスの空燃比がリーン
になるとNOx がNOx 吸放出触媒10に吸収され、流
入排気ガスの空燃比をリッチにするとNOx がNOx 吸
放出触媒10から短時間のうちに放出されて還元され
る。ディーゼル機関では、通常、排気ガスはリッチまた
はストイキとなることがなく、常にリーンである。そこ
で、NOx 吸放出触媒10に吸収されたNOx を放出し
て還元する場合には、燃料供給装置14から排気通路6
内に燃料を供給するようにしている。供給された燃料は
NOx 吸放出触媒10で燃焼せしめられ、これによって
NOx 吸放出触媒10内の排気ガス中の酸素が消費され
て酸素濃度が低下し、このため、NOx 吸放出触媒10
からNOx が放出されて還元浄化される。As described above, when the air-fuel ratio of the inflowing exhaust gas becomes lean, NOx is absorbed by the NOx adsorbing / releasing catalyst 10, and when the air-fuel ratio of the inflowing exhaust gas is made rich, NOx is released from the NOx adsorbing / releasing catalyst 10 within a short time. Released and reduced. In a diesel engine, the exhaust gas is not always rich or stoichiometric, and is always lean. Therefore, when the NOx absorbed and released by the NOx absorption / desorption catalyst 10 is released and reduced, the fuel supply device 14 supplies the NOx to the exhaust passage 6.
The fuel is supplied inside. The supplied fuel is burned by the NOx adsorbing / releasing catalyst 10, whereby the oxygen in the exhaust gas in the NOx adsorbing / releasing catalyst 10 is consumed and the oxygen concentration is reduced.
NOx is released from the gas and is reduced and purified.
【0014】ところが、排気ガス温度が低くNOx 吸放
出触媒10が活性温度に達していない場合には、排気通
路6内に供給された燃料はNOx 吸放出触媒10で燃焼
しないために、排気ガス中の酸素量が低下せず、この結
果、NOx 吸放出触媒からNOx が放出されず、あるい
はNOx が放出されても十分に還元浄化されないという
問題を生ずる。However, when the temperature of the exhaust gas is low and the NOx adsorbing / releasing catalyst 10 has not reached the activation temperature, the fuel supplied into the exhaust passage 6 does not burn in the NOx adsorbing / releasing catalyst 10, so that the As a result, there arises a problem that NOx is not released from the NOx adsorbing and releasing catalyst, or even if NOx is released, it is not sufficiently reduced and purified.
【0015】そこで第1の実施例では、図3に示される
ように、NOx 吸放出触媒10の上流側端部10aに白
金Ptを高担持させると共に他の部分10bには白金P
tを通常量だけ担持させている。これによって、上流側
端部10aの触媒活性温度を低下させることができ、従
って、排気ガス温度が低い場合であっても、燃料をNO
x 吸放出触媒10の上流側端部10aで燃焼開始せしめ
ることができる。上流側端部10aで燃料が燃焼開始せ
しめられると、その発生熱によってNOx 吸放出触媒1
0の他の部分10bも加熱されて触媒活性温度以上とな
り燃料が燃焼開始せしめられる。これによって、NOx
吸放出触媒10内の排気ガス中の酸素が消費されて酸素
濃度が低下し、このため、NOx 吸放出触媒10からN
Ox が放出されて還元浄化される。Therefore, in the first embodiment, as shown in FIG. 3, platinum Pt is carried on the upstream end portion 10a of the NOx adsorbing / releasing catalyst 10 at a high level, and platinum Pt is carried on the other portion 10b.
t is carried in an ordinary amount. As a result, the catalyst activation temperature at the upstream end portion 10a can be lowered, and therefore, even if the exhaust gas temperature is low, the fuel can be reduced to NO.
x The combustion can be started at the upstream end 10a of the adsorption / desorption catalyst 10. When the combustion of the fuel is started at the upstream end portion 10a, the NOx absorption / desorption catalyst 1 is generated by the generated heat.
The other portion 10b of 0 is also heated to a temperature equal to or higher than the catalyst activation temperature, and combustion of the fuel is started. As a result, NOx
Oxygen in the exhaust gas in the adsorption / desorption catalyst 10 is consumed and the oxygen concentration is reduced.
Ox is released and reduced and purified.
【0016】次に第2の実施例について説明する。第2
の実施例では、NOx 吸放出触媒10に吸収されたNO
x を放出して還元する場合であって、NOx 吸放出触媒
10が活性温度に達していない場合には、吸気絞り弁8
の開度を絞り、これによって吸入空気量を減少せしめる
ようにしている。この結果、NOx 吸放出触媒10に流
入する排気ガス温度が上昇せしめられてNOx 吸放出触
媒10が活性温度に達し、排気通路に供給された燃料が
燃焼開始せしめられる。燃料が燃焼開始すればその発生
熱によってNOx 吸放出触媒10は活性温度以上に維持
されるために、吸気絞り弁8の開度を絞るのは、燃料の
燃焼開始時期だけでよい。なお、吸気絞り弁8の絞り量
は、機関運転上支障ない程度に吸入空気量が減少するよ
うにされている。Next, a second embodiment will be described. Second
In the embodiment, the NOx absorbed and released by the
When the NOx adsorbing / releasing catalyst 10 has not reached the activation temperature in the case of reducing by releasing x, the intake throttle valve 8
Of the intake air is reduced, thereby reducing the intake air amount. As a result, the temperature of the exhaust gas flowing into the NOx adsorbing / releasing catalyst 10 is increased, the NOx adsorbing / releasing catalyst 10 reaches the activation temperature, and the fuel supplied to the exhaust passage is started to burn. When the fuel starts burning, the NOx adsorbing / releasing catalyst 10 is maintained at a temperature equal to or higher than the activation temperature by the generated heat. Therefore, the opening degree of the intake throttle valve 8 may be reduced only at the fuel combustion starting time. The throttle amount of the intake throttle valve 8 is set so that the intake air amount is reduced to such an extent that the operation of the engine is not hindered.
【0017】次に第3の実施例について説明する。第3
の実施例では、NOx 吸放出触媒10上流のケーシング
12内に電気式ヒータ16が配置されている。NOx 吸
放出触媒10に吸収されたNOx を放出して還元する場
合であって、NOx 吸放出触媒10が活性温度に達して
いない場合には、ヒータ16に通電せしめてNOx 吸放
出触媒10を活性温度以上とする。なおヒータ16への
通電は、NOx 吸放出触媒10で燃料が燃焼開始すると
きだけでよい。Next, a third embodiment will be described. Third
In the embodiment, the electric heater 16 is disposed in the casing 12 upstream of the NOx absorption / release catalyst 10. When the NOx absorbed and released by the NOx absorption and release catalyst 10 is released and reduced, and the NOx absorption and release catalyst 10 has not reached the activation temperature, the heater 16 is energized to activate the NOx absorption and release catalyst 10. It should be higher than the temperature. The heater 16 needs to be energized only when the fuel starts to be burned by the NOx absorption / release catalyst 10.
【0018】なお、燃焼促進手段は上述のものに限られ
ず、NOx 吸放出触媒10に吸収されたNOx を放出し
て還元する場合であって、NOx 吸放出触媒10が活性
温度に達していない場合には、NOx 吸放出触媒10上
流に水素、プロピレン、プロパン等の反応性の良いガス
またはガソリンのように揮発性の高い液体を注入しても
よいし、また、電気的負荷(オルタネータ、ブロア等)
または物理的負荷(エアコン、トルクコンバータ等)を
増大せしめて排気ガス温度を高めるようにしてもよい。Note that the combustion promoting means is not limited to the above-described one, but is a case where the NOx absorbed and released by the NOx absorbing and releasing catalyst 10 is released and reduced, and the NOx absorbing and releasing catalyst 10 does not reach the activation temperature. A highly reactive gas such as hydrogen, propylene, propane, or a highly volatile liquid such as gasoline may be injected upstream of the NOx absorption / desorption catalyst 10, and an electric load (alternator, blower, etc.) )
Alternatively, the physical load (air conditioner, torque converter, etc.) may be increased to increase the exhaust gas temperature.
【0019】なお、本実施例ではディーゼル機関につい
て説明したが、本発明はガソリン機関にも適用すること
ができる。Although the present embodiment has been described with reference to a diesel engine, the present invention can also be applied to a gasoline engine.
【0020】[0020]
【発明の効果】NOx 吸放出触媒の上流側端部における
白金の担持量をその他の部分における白金の担持量より
も多くすることによって排気ガスが低温であっても、還
元剤の燃焼開始が促進され、NOx を確実に還元せしめ
ることができる。Effect of the Invention At the upstream end of the NOx absorption / release catalyst
The supported amount of platinum is calculated from the supported amount of platinum in other parts.
When the exhaust gas temperature is low, the start of combustion of the reducing agent is promoted, and NOx can be reliably reduced.
【図1】本発明の実施例の内燃機関の全体図である。FIG. 1 is an overall view of an internal combustion engine according to an embodiment of the present invention.
【図2】NOx の吸放出作用を説明するための図であ
る。FIG. 2 is a diagram for explaining an absorption / release effect of NOx.
【図3】本発明の第1の実施例のNOx 吸放出触媒を示
す図である。FIG. 3 is a view showing a NOx absorption / release catalyst according to a first embodiment of the present invention.
【図4】本発明の第3の実施例のNOx 吸放出触媒を示
す図である。FIG. 4 is a view showing a NOx storage / release catalyst according to a third embodiment of the present invention.
2…ディーゼル機関本体 6…排気通路 8…吸気絞り弁 10…NOx 吸放出触媒 14…燃料供給装置 2: Diesel engine body 6: Exhaust passage 8: Intake throttle valve 10: NOx absorption / release catalyst 14: Fuel supply device
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F01N 3/08 F01N 3/18 F01N 3/28 301──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 6 , DB name) F01N 3/08 F01N 3/18 F01N 3/28 301
Claims (1)
Ox を吸収し排気ガスの空燃比がストイキまたはリッチ
のときには吸収したNOx を放出すると共に放出された
NOx を還元するNOx 吸放出触媒を機関排気通路内に
配置し、前記NOx 吸放出触媒からNOx を放出せしめ
て還元せしめるときには前記NOx 吸放出触媒に還元剤
を供給して燃焼せしめ、前記NOx 吸放出触媒での還元
剤の燃焼開始を促進するためにNOx 吸放出触媒の上流
側端部における白金の担持量をその他の部分における白
金の担持量よりも多くした内燃機関の排気浄化装置。1. When the air-fuel ratio of exhaust gas is lean, N
When the air-fuel ratio of the exhaust gas is stoichiometric or rich, a NOx absorbing / releasing catalyst for releasing the absorbed NOx and reducing the released NOx is disposed in the engine exhaust passage, and the NOx absorbing / releasing catalyst removes the NOx from the NOx absorbing / releasing catalyst. At the time of release and reduction, a reducing agent is supplied to the NOx absorption / release catalyst to burn it, and upstream of the NOx absorption / release catalyst to promote the start of combustion of the reducing agent at the NOx absorption / release catalyst.
The amount of platinum carried on the side
An exhaust gas purification device for an internal combustion engine that has a larger amount of gold carried .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25830692A JP2845052B2 (en) | 1992-09-28 | 1992-09-28 | Exhaust gas purification device for internal combustion engine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25830692A JP2845052B2 (en) | 1992-09-28 | 1992-09-28 | Exhaust gas purification device for internal combustion engine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06108826A JPH06108826A (en) | 1994-04-19 |
| JP2845052B2 true JP2845052B2 (en) | 1999-01-13 |
Family
ID=17318425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25830692A Expired - Lifetime JP2845052B2 (en) | 1992-09-28 | 1992-09-28 | Exhaust gas purification device for internal combustion engine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2845052B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4158697B2 (en) | 2003-06-17 | 2008-10-01 | トヨタ自動車株式会社 | Exhaust gas purification device and exhaust gas purification method for internal combustion engine |
| JP3912354B2 (en) | 2003-10-10 | 2007-05-09 | トヨタ自動車株式会社 | Exhaust purification device and exhaust purification method for internal combustion engine |
| US7673445B2 (en) * | 2004-11-09 | 2010-03-09 | Ford Global Technologies, Llc | Mechanical apparatus having a catalytic NOx storage and conversion device |
-
1992
- 1992-09-28 JP JP25830692A patent/JP2845052B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06108826A (en) | 1994-04-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP2605556B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2605553B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2586738B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2760251B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP3093905B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2605559B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP3580180B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2845052B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP3353650B2 (en) | Catalyst poisoning regeneration equipment for internal combustion engines | |
| JP2658756B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JPH0650132A (en) | Exhaust gas purification device for internal combustion engine | |
| JP2743751B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP3514200B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP3397175B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2746029B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2842135B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2000080913A (en) | Exhaust gas purification device for internal combustion engine | |
| JP2663807B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP3385974B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2605571B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP2830665B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP4269919B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JP3496572B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JPH06108828A (en) | Exhaust gas purification device for internal combustion engine | |
| JP2852589B2 (en) | Exhaust gas purification device for internal combustion engine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 10 Free format text: PAYMENT UNTIL: 20081030 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20081030 Year of fee payment: 10 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20091030 Year of fee payment: 11 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 11 Free format text: PAYMENT UNTIL: 20091030 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 12 Free format text: PAYMENT UNTIL: 20101030 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20101030 Year of fee payment: 12 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111030 Year of fee payment: 13 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111030 Year of fee payment: 13 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 14 Free format text: PAYMENT UNTIL: 20121030 |
|
| EXPY | Cancellation because of completion of term |