JPH0374513A - Exhaust gas purification device for diesel engine - Google Patents

Exhaust gas purification device for diesel engine

Info

Publication number
JPH0374513A
JPH0374513A JP20914989A JP20914989A JPH0374513A JP H0374513 A JPH0374513 A JP H0374513A JP 20914989 A JP20914989 A JP 20914989A JP 20914989 A JP20914989 A JP 20914989A JP H0374513 A JPH0374513 A JP H0374513A
Authority
JP
Japan
Prior art keywords
exhaust gas
catalyst
purification catalyst
air
fuel ratio
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.)
Pending
Application number
JP20914989A
Other languages
Japanese (ja)
Inventor
Hisayuki Yamane
久幸 山根
Tsugio Hatsuhira
次男 服平
Hirobumi Yamauchi
山内 博文
Hiroshi Murakami
浩 村上
Kazuya Komatsu
一也 小松
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.)
Mazda Motor Corp
Original Assignee
Mazda 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 Mazda Motor Corp filed Critical Mazda Motor Corp
Priority to JP20914989A priority Critical patent/JPH0374513A/en
Publication of JPH0374513A publication Critical patent/JPH0374513A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B3/00Engines characterised by air compression and subsequent fuel addition
    • F02B3/06Engines characterised by air compression and subsequent fuel addition with compression ignition

Abstract

PURPOSE:To prolong the service life of a NOx purifying catalyst by providing a particulate removing device on the upstream side of the NOx purifying cata lyst, and a catalyst protecting means operated when exhaust gas temperature exceeds a specified valve and air-fuel ratio becomes richer than a specified value. CONSTITUTION:A catalyst 20 to purify NOx in exhaust gas is placed on the way of an exhaust pipe 18 of a diesel engine. A particulate filter 21 for trapping particulates in exhaust gas is placed on the upstream side of the catalyst 20. A particulate remover 23 is constituted with both components 21, 22 so that particulates adhering to the filter 21 can be burned with the burner 22. A secon dary air passage 38 is connected to an exhaust pipe 18 located between the filter 21 and the catalyst 20, and a secondary air pump 36 is connected via a secondary air control valve 40 to the upstream side of the pipe 38 to constitute a catalyst protecting device 46. The valve 40 is opened when air-fuel ratio exceeds a specified value with exhaust gas temperature above a specified value so that the exhaust gas temperature is lowered for preventing the catalyst 20 from deteriorating.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はディーゼルエンジンの排気ガス浄化装置の改良
に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an improvement in an exhaust gas purification device for a diesel engine.

(従来の技術) ディーゼルエンジンは空燃比のリーン状態で運転される
ためガソリンエンジンのように排気ガス中の1(CやC
Oは余り多くないが、排気ガス中のNOxは、酸性雨を
降らせる原因になる等の理由によって問題になる。この
ため、ディーゼルエンジンでは、排気ガス中のNOxの
浄化が切に望まれている。
(Prior art) Diesel engines are operated with a lean air-fuel ratio, so unlike gasoline engines, 1 (C and C) in the exhaust gas is
Although there is not much O, NOx in the exhaust gas becomes a problem because it causes acid rain. For this reason, in diesel engines, it is strongly desired to purify NOx in exhaust gas.

これに対して、排気ガス中のNOxを浄化する方法とし
てN)13接触還元法が知られているが、このNH3接
触還元法は、システムが複雑でコストが高い上に、燃焼
ガス温度が高い時にNH3が排出されるという二次公害
の問題を有しているため、自動車に適用するには未解決
の問題が多い。
On the other hand, the N)13 catalytic reduction method is known as a method for purifying NOx in exhaust gas, but this NH3 catalytic reduction method has a complicated system and high cost, and the combustion gas temperature is high. There are many unresolved problems in applying it to automobiles because it sometimes causes secondary pollution due to NH3 being emitted.

そこで、近時、特開昭63−100919号公報に示さ
れるように、酸化雰囲気中、HCの存在下でNOxを浄
化することができる触媒としてCUを含有するNOx浄
化触媒が提案されている。
Therefore, as disclosed in Japanese Patent Application Laid-Open No. 63-100919, a NOx purification catalyst containing CU has been proposed as a catalyst capable of purifying NOx in the presence of HC in an oxidizing atmosphere.

(発明が解決しようとする課題) しかるに、このCuを含有するNOx浄化触媒は、排気
ガスの空燃比がリーンな状態でNOxを効果的に浄化で
きる反面、排気ガスの温度が高く且つ排気ガスの空燃比
がリッチのときには、NOx浄化触媒の銅イオンが金属
銅に還元されて活性を失うという問題がある。
(Problem to be Solved by the Invention) However, although this NOx purification catalyst containing Cu can effectively purify NOx when the air-fuel ratio of the exhaust gas is lean, the exhaust gas temperature is high and the exhaust gas When the air-fuel ratio is rich, there is a problem that the copper ions of the NOx purification catalyst are reduced to metallic copper and lose their activity.

また、前記のNOx浄化触媒は、第6図に示すように、
排気ガス温度によって浄化性能が穴なり、排気ガス温度
が500℃付近のときに浄化性能がピークで、この温度
以上或いは以下では浄化性能が低下するという問題も有
している。
Further, as shown in FIG. 6, the NOx purification catalyst described above has the following characteristics:
There is also the problem that the purification performance varies depending on the exhaust gas temperature, and the purification performance peaks when the exhaust gas temperature is around 500° C., and the purification performance decreases above or below this temperature.

前記に鑑み、本発明は、排気ガスの温度が高く且つ空燃
比がリッチのときでも、NOx浄化触媒が劣化しないよ
うにすることを目的とする。
In view of the above, an object of the present invention is to prevent the NOx purification catalyst from deteriorating even when the exhaust gas temperature is high and the air-fuel ratio is rich.

(課題を解決するための手段) 前記の目的を達成するため、請求項(1)の発明は、N
Ox浄化触媒上流の排気ガスの温度及び空燃比を検出し
、この排気ガスがNOx浄化触媒を劣化させる雰囲気の
ときに、NOx浄化触媒の雰囲気を劣化しない雰囲気に
するものである。
(Means for solving the problem) In order to achieve the above object, the invention of claim (1)
The temperature and air-fuel ratio of the exhaust gas upstream of the Ox purification catalyst are detected, and when the exhaust gas is in an atmosphere that degrades the NOx purification catalyst, the atmosphere of the NOx purification catalyst is made to be an atmosphere that does not deteriorate.

具体的に請求項(1)の発明の講じた解決手段は、排気
系にCuを含有するNOx浄化触媒を備えたディーゼル
エンジンの排気ガス浄化装置を前提とし、前記NOx触
媒の上流に配設され、排只ガス中の微粒子を捕集し且つ
燃焼させる微粒子除去装置と、前記NOx浄化触媒の雰
囲気を劣化しない雰囲気にする触媒保護手段と、前記N
Ox浄化触媒に流入する排気ガスの温度を検出する排気
ガス温度センサと、前記NOx浄化触媒上流側の排気ガ
スの空燃比を検出する空燃比検出手段と、前記排気ガス
温度センサ及び空燃比検出手段からの出力信号を受け、
前記排気ガスの温度が所定値以上に高くなり且つ空燃比
が所定以上リッチになると前記触媒保護手段を作動させ
る制御手段とを備える構成とするものである。
Specifically, the solution taken by the invention of claim (1) is based on an exhaust gas purification device for a diesel engine equipped with a NOx purification catalyst containing Cu in the exhaust system, and is provided upstream of the NOx catalyst. , a particulate removal device that collects and burns particulates in exhaust gas, a catalyst protection means that makes the atmosphere of the NOx purification catalyst an atmosphere that does not deteriorate;
an exhaust gas temperature sensor that detects the temperature of exhaust gas flowing into the Ox purification catalyst; an air-fuel ratio detection means that detects the air-fuel ratio of the exhaust gas upstream of the NOx purification catalyst; and the exhaust gas temperature sensor and air-fuel ratio detection means. receives the output signal from
The apparatus further includes a control means for operating the catalyst protection means when the temperature of the exhaust gas becomes higher than a predetermined value and the air-fuel ratio becomes richer than a predetermined value.

また、請求項(2]の発明では、NOx浄化触媒の劣化
を防止すると共にNOx浄化触媒の浄化性能を向上させ
るため、前記触媒保護手段をNOx浄化触媒の上流に二
次エアを供給する二次エア供給装置としたものである。
In addition, in the invention of claim (2), in order to prevent deterioration of the NOx purification catalyst and improve the purification performance of the NOx purification catalyst, the catalyst protection means is provided as a secondary air purifier for supplying secondary air upstream of the NOx purification catalyst. This is an air supply device.

(作用) 請求項(1)の発明の構成により、NOx触媒の上流側
に微粒子除去装置が配設されているので、排気ガス中の
微粒子はNOx浄化触媒に達する前に捕集され、NOx
浄化触媒に達しない。
(Function) According to the configuration of the invention of claim (1), since the particulate removal device is disposed upstream of the NOx catalyst, particulates in the exhaust gas are collected before reaching the NOx purification catalyst, and NOx
It does not reach the purification catalyst.

また、排気ガスの温度が所定値以上に高くなり且つ空燃
比が所定以上リッチになると、触媒保護手段を作動させ
る制御手段を備えているため、エンジンが高負荷状態で
運転されたり、或いは、微粒子除去装置に捕集された微
粒子が燃焼したりして、NOx浄化触媒上流側の排気ガ
スの温度が所定値以上に高くなり且つ空燃比が設定以上
1ルソチになると、つまりNOx浄化触媒が劣化する領
域になると、触媒保護手段が作動してNOx浄化触媒の
雰囲気を劣化しない雰囲気にする。
In addition, the engine is equipped with a control means that activates the catalyst protection means when the exhaust gas temperature rises above a predetermined value and the air-fuel ratio becomes richer than a predetermined value. When the particulates collected by the removal device burn, and the temperature of the exhaust gas upstream of the NOx purification catalyst becomes higher than a predetermined value, and the air-fuel ratio exceeds the set value by 1 Rusoti, that is, the NOx purification catalyst deteriorates. In this range, the catalyst protection means is activated to make the atmosphere around the NOx purification catalyst an atmosphere that does not deteriorate.

また、請求項(2)の発明の構成により、NOx浄化触
媒上流側の排気ガスの温度が所定値以上に高(なり且つ
空燃比が設定以上リッチになると、二次エア供給装置が
NOx浄化装置の上流に二次エアを供給するため、排気
ガスの空燃比がリーン傾向になってNOx浄化触媒の劣
化が防止されると共に、排気ガスの温度が低下してNO
x浄化触媒の浄化性能が向上する。
Further, according to the configuration of the invention of claim (2), when the temperature of the exhaust gas on the upstream side of the NOx purification catalyst becomes higher than a predetermined value (and the air-fuel ratio becomes richer than the set value), the secondary air supply device Since secondary air is supplied upstream of the exhaust gas, the air-fuel ratio of the exhaust gas tends to be lean, preventing deterioration of the NOx purification catalyst, and the temperature of the exhaust gas decreases, reducing the NOx purification catalyst.
x The purification performance of the purification catalyst is improved.

(実施例) 以下、本発明の実施例を図面に基づいて説明する。(Example) Embodiments of the present invention will be described below based on the drawings.

第1図は、本発明の第1実施例に係るディーゼルエンジ
ンの排気ガス浄化装置がディーゼルエンジン10に適用
された場合の仝体構成を示し、同図において、12はデ
ィーゼルエンジン10にエアを吸入するための吸気管、
14はディーゼルエンジン10の各シリンダへエアを配
給するインテークマニホールド、15は前記各シリンダ
に燃料を噴射、供給する燃料噴射ポンプ、16は前記各
シリンダから排出される排気ガスを集めるエキゾースト
マニホールド、18は排気ガスを排出する排気管である
FIG. 1 shows a body structure when the exhaust gas purification device for a diesel engine according to the first embodiment of the present invention is applied to a diesel engine 10. Intake pipe for
14 is an intake manifold that distributes air to each cylinder of the diesel engine 10; 15 is a fuel injection pump that injects and supplies fuel to each cylinder; 16 is an exhaust manifold that collects exhaust gas discharged from each cylinder; 18 is an exhaust manifold that collects exhaust gas discharged from each cylinder; This is an exhaust pipe that discharges exhaust gas.

また、同図において、20は排気ガス中のNOxを還元
するNOx浄化触媒であって、次のようにして製造され
る。すなわち、ゼオライトの一種であるモルデナイト[
Na20−Al!03 ・n5t02コのNaがHで置
換され、5i02/A1:Oiのモル比が10以上で、
細孔径が7オングストロ一ム程度のものを準備し、これ
を有機酸鋼の水溶液に含浸させ、イオン交換を起こさせ
てCuを担持させる。この場合、銅イオン交換率が多い
ものほどNOxの浄化率は高いと共に、5tO=/A1
2(hのモル比が高いほど触媒活性が高い。
Further, in the same figure, 20 is a NOx purification catalyst that reduces NOx in exhaust gas, and is manufactured as follows. In other words, mordenite, a type of zeolite [
Na20-Al! 03 ・Na of n5t02 is replaced with H, and the molar ratio of 5i02/A1:Oi is 10 or more,
A material with a pore diameter of approximately 7 angstroms is prepared, and is impregnated with an aqueous solution of organic acid steel to cause ion exchange and support Cu. In this case, the higher the copper ion exchange rate, the higher the NOx purification rate, and 5tO=/A1
2(The higher the molar ratio of h, the higher the catalytic activity.

また、このNOx浄化触媒20は、2Cu  +NO−
2Cu2”+N0−=2Cu” +N2 +02に示さ
れる分解反応をすることによりNoをNごと02に分解
するものであって、前記のように500℃前後でNOに
対する高い浄化率を有していると共に、他の触媒に比べ
てNo分解性能がかなり高い。
Further, this NOx purification catalyst 20 has 2Cu +NO-
2Cu2"+N0-=2Cu" +N2 +02 It decomposes NO into 02 along with N, and as mentioned above, it has a high purification rate for NO at around 500℃ and also , has significantly higher No decomposition performance than other catalysts.

また、同図において、21はNOx浄化触媒20の上流
側の排気管18に配設され、排気ガス中の微粒子を捕集
して濾過するDPF (ディーゼルパティキュレートフ
ィルター)、22はDPF21の上流側の排気管18の
壁部に配設され、DPF21に付着した微粒子を燃焼さ
せるバーナーであって、これらDPF21及びバーナー
22によって、排気ガス中の微粒子を捕集すると共に捕
集した微粒子を燃焼させて除去する微粒子除去装置23
が構成されている。
In addition, in the same figure, 21 is a DPF (diesel particulate filter) disposed in the exhaust pipe 18 upstream of the NOx purification catalyst 20 to collect and filter particulates in the exhaust gas, and 22 is a DPF 21 upstream of the DPF 21. This burner is disposed on the wall of the exhaust pipe 18 and burns particulates adhering to the DPF 21.The DPF 21 and burner 22 collect particulates in the exhaust gas and burn the collected particulates. Particulate removal device 23 to remove
is configured.

このようにして、NOx浄化触媒20の上流側1:DP
F21が配設されているので、排気ガス中の微粒子はD
PF21によって捕集されてNOx浄化触媒20に達し
ないため、NOx浄化触媒20の浄化性能の低下が防止
される。
In this way, the upstream side 1:DP of the NOx purification catalyst 20
Since F21 is installed, fine particles in the exhaust gas are
Since it is collected by the PF 21 and does not reach the NOx purification catalyst 20, deterioration in the purification performance of the NOx purification catalyst 20 is prevented.

また、DPF21の上流側にバーナー22が配設されて
いるので、DPF21に微粒子が多く付着して排気ガス
の流通状態が悪化したときに、バーナー22により微粒
子を燃焼、除去できる。
Further, since the burner 22 is disposed upstream of the DPF 21, when a large number of particles adhere to the DPF 21 and the exhaust gas flow condition deteriorates, the burner 22 can burn and remove the particles.

なお、付着した微粒子を燃焼させる手段は、バーナー2
2に限られず、DPF21に配設されたヒータ或いは高
周波誘導加熱手段でもよい。
Incidentally, the means for burning the attached particulates is the burner 2.
2, a heater disposed in the DPF 21 or a high frequency induction heating means may be used.

また、前記の場合、DPF21に付着した微粒子を燃焼
しやすくするため、DPF21のフィルターに触媒をコ
ートしておき、微粒子の燃焼温度を低下させることもで
きる。
Further, in the above case, in order to make it easier to burn the particulates attached to the DPF 21, the filter of the DPF 21 can be coated with a catalyst to lower the combustion temperature of the particulates.

また、第1図及び第2図において、24はDPF21の
上流側及びNOx浄化触媒20の下流側の排気管18と
、吸気管12とを連通させ、排気ガスを排気管18から
吸気管12へと還流させるEGR通路、26A、26B
は排気管18との連通部近傍のEGR通路24に介設さ
れ、EGR通路24を還流する排気ガス量を可変するE
GRパルプ、28A、28Bはオルタネータに装着され
た真空ポンプ29とEGRバルブ26A、26Bとを連
通させ、EGRパルプ26A、26Bに負圧を導入する
負圧導入通路、30A、30Bは負圧導入通路28A、
28Bに介設され、EGRバルブ26A、26Bの開度
をデユーティ制御により調節するEGR用ソレノイドバ
ルブである。
In FIGS. 1 and 2, 24 communicates the exhaust pipe 18 upstream of the DPF 21 and downstream of the NOx purification catalyst 20 with the intake pipe 12, and directs the exhaust gas from the exhaust pipe 18 to the intake pipe 12. and EGR passages, 26A, 26B that recirculate
is interposed in the EGR passage 24 near the communication part with the exhaust pipe 18, and is used to vary the amount of exhaust gas recirculated through the EGR passage 24.
GR pulp, 28A, 28B is a negative pressure introduction passage that communicates the vacuum pump 29 attached to the alternator with the EGR valves 26A, 26B, and introduces negative pressure into the EGR pulp 26A, 26B; 30A, 30B are negative pressure introduction passages. 28A,
This is an EGR solenoid valve that is installed in EGR valve 28B and adjusts the opening degree of EGR valves 26A and 26B by duty control.

以上説明したEGR通路24、EGRバルブ26A、2
6B、負圧導入通路28A、28B、真空ポンプ29及
びEGR用ソリソレノイドバルブ30A0BによってE
GR装置32が構成されており、このEGR装置32に
より、排気ガスが吸気系に還流されて燃焼室の熱容量が
高められる結果、排気ガス中に排出されるNOxが低減
する。
The EGR passage 24 and EGR valves 26A and 2 explained above
6B, negative pressure introduction passages 28A, 28B, vacuum pump 29, and EGR solenoid valve 30A0B.
A GR device 32 is configured, and as a result of this EGR device 32, exhaust gas is recirculated to the intake system and the heat capacity of the combustion chamber is increased, NOx discharged into the exhaust gas is reduced.

この場合、エンジンの低負荷時にはDPF21の上流側
から排気ガスを取出し、エンジンの高負荷時にはNOx
浄化触媒20の下流側から排気ガスを取出すようにEG
R用ソリソレノイドパルプ30A0Bを各々制御する。
In this case, when the engine is under low load, exhaust gas is extracted from the upstream side of the DPF 21, and when the engine is under high load, NOx
EG so as to extract exhaust gas from the downstream side of the purification catalyst 20.
Each of the R soli solenoid pulps 30A0B is controlled.

このようにすると、エンジンの低負荷時には、DPF2
1の上流側から排気ガスを取出すことにより高温の排気
ガスが得られ、エンジンの燃焼性が向上する。また、エ
ンジンの高負荷時には、排気ガスがNOx浄化触媒20
を通過することにより、NOxが02とN2とに分解さ
れ、比熱の高い排気ガスが吸気系に還流されるので、燃
焼温度が低下してNOxの排出量は低減する。
In this way, when the engine is under low load, DPF2
By extracting exhaust gas from the upstream side of engine 1, high-temperature exhaust gas is obtained, improving the combustibility of the engine. In addition, when the engine is under high load, exhaust gas is
By passing through the exhaust gas, NOx is decomposed into 02 and N2, and the exhaust gas with high specific heat is returned to the intake system, so the combustion temperature is lowered and the amount of NOx emissions is reduced.

また、本実施例では、吸気管12におけるEGR通路2
4との連通部より上流側に吸気絞り弁12aが配設され
ている。その理由は、ディーゼルエンジンでは、吸気圧
と排気圧との差が小さいため、排気ガスがEGRa路2
4から吸気管12へ流入しにくい。そこで、排気ガスを
還流する際、この吸気絞り弁12aを絞って所定の吸気
圧にし、排気ガスを還流させ易くするためである。もっ
とも、この場合でも、排気ガスの還流量はEGRバルブ
26A、26Bの開度を調節することによって:J8!
lする。
Further, in this embodiment, the EGR passage 2 in the intake pipe 12
An intake throttle valve 12a is disposed on the upstream side of the communication portion with 4. The reason for this is that in diesel engines, the difference between intake pressure and exhaust pressure is small, so exhaust gas is
4 into the intake pipe 12. Therefore, when the exhaust gas is recirculated, the intake throttle valve 12a is throttled to a predetermined intake pressure to facilitate the recirculation of the exhaust gas. However, even in this case, the amount of exhaust gas recirculation can be adjusted by adjusting the opening degrees of the EGR valves 26A and 26B: J8!
I do it.

また、第1図において、36は二次エアの供給源である
エアポンプ、38はエアポンプ36と、DPF21とN
Ox浄化触媒20との間の排気管18とを連通させ、二
次エアを排気管18へ供給するための二次エア通路、4
0は二次エア通路36を流通する二次エア量を可変する
二次エア調整バルブ、42は前記の真空ポンプ29と二
次エア調整バルブ40とを連通し、二次エア調整バルブ
40に負圧を供給する負圧導入通路、44は負圧導入通
路42に介設され、二次エア調整バルブ40の開度をデ
ユーティ制御により調節する二次エア用ソレノイドバル
ブであって、以上説明した二次エアポンプ36、二次エ
ア通路38、二次エア調整バルブ40、負圧導入通路4
2及び二次エア用ソレノイドバルブ44によって、NO
x浄化触媒20の上流に二次エアを供給する二次エア供
給装置46が構成されている。そして、この二次エア供
給袋rrt46はNOx浄化触媒20の劣化を防止する
触媒保護手段を構成しており、二次エア供給装置46に
よって排気ガス中に二次エアが供給されると、NOx浄
化触媒20に流入する排気ガスの温度が低下すると共に
空燃比がリーン傾向になる。
Further, in FIG. 1, 36 is an air pump which is a supply source of secondary air, 38 is an air pump 36, DPF 21 and N
a secondary air passage 4 for communicating with the exhaust pipe 18 between the Ox purification catalyst 20 and supplying secondary air to the exhaust pipe 18;
0 is a secondary air adjustment valve that varies the amount of secondary air flowing through the secondary air passage 36; 42 is a secondary air adjustment valve that communicates with the vacuum pump 29 and the secondary air adjustment valve 40; The negative pressure introduction passage 44 that supplies pressure is a secondary air solenoid valve that is interposed in the negative pressure introduction passage 42 and adjusts the opening degree of the secondary air adjustment valve 40 by duty control. Secondary air pump 36, secondary air passage 38, secondary air adjustment valve 40, negative pressure introduction passage 4
2 and secondary air solenoid valve 44, NO.
A secondary air supply device 46 is configured to supply secondary air upstream of the x purification catalyst 20. This secondary air supply bag rrt46 constitutes a catalyst protection means for preventing deterioration of the NOx purification catalyst 20, and when secondary air is supplied into the exhaust gas by the secondary air supply device 46, NOx purification is performed. As the temperature of the exhaust gas flowing into the catalyst 20 decreases, the air-fuel ratio tends to lean.

このようにして、ディーゼルエンジン10が高負荷状態
のため排気ガスがリッチで高温になったり、或いはバー
ナー22等によってDPF21に付着した微粒子が燃焼
する際の熱で排気ガスか高温になったりしても、二次エ
アを供給することにより、排気ガスの空燃比をリーン傾
向にさせると共に排気ガスの温度を低下させることがで
きる。
In this way, the exhaust gas becomes rich and high temperature because the diesel engine 10 is in a high load state, or the exhaust gas becomes high temperature due to the heat generated when particulates attached to the DPF 21 are burned by the burner 22 or the like. Also, by supplying secondary air, the air-fuel ratio of the exhaust gas tends to be lean, and the temperature of the exhaust gas can be lowered.

このため、排気ガスがリッチで且つ高温のときに、NO
x浄化触媒20の銅イオンが金属銅に還元されて活性を
失い、NOx浄化触120が劣化する事態を防止できる
ので、NOx浄化触媒20の保護が図られる。また、排
気ガスの温度が低下することにより、NOx浄化触媒2
0の浄化性能の向上も図られる。
Therefore, when the exhaust gas is rich and high temperature, NO
Since it is possible to prevent the copper ions of the x purification catalyst 20 from being reduced to metallic copper and losing activity and the NOx purification catalyst 120 deteriorating, the NOx purification catalyst 20 is protected. In addition, as the temperature of the exhaust gas decreases, the NOx purification catalyst 2
0 purification performance can also be improved.

また、第1図において、50はエンジン冷却水温度を検
出する冷却水温度センサ、51はエンジンの吸気温度を
検出する吸気温度センナ、52はエンジンの吸気圧を検
出する吸気圧センサ、54はNOx浄化触媒22上流側
の排気ガスの温度を検出する排気ガス温度センサ、55
はNOx浄化触媒に流入する排気ガスの空燃比を検出す
る空燃比検出手段としての02センサ、56は排気ガス
の圧力を検出する圧力センサであって、この圧力センサ
56によりDPF21のフィルターに微粒子が多く付着
してフィルターが目づまりを起こしている状態を検知で
きる。 また、第1図において、60はCPU内蔵のコ
ントロールユニットであって、冷却水温度センサ50か
らエンジン冷却水温度信号、吸気温度センサ51からエ
ンジンの吸気温度信号、吸気圧センサ52からのエンジ
ンの吸気圧信号、排気ガス温度センサ54から排気ガス
温度信号、02センサ55からの排気ガスの空燃比信号
、圧力センサ56からの排気ガス圧力信号、燃料噴射ポ
ンプ15からのエンジン回転数信号及びエンジン負荷信
号等を受け、エンジン回転数信号及びエンジン負荷信号
に基づきEGR装置232を作動させるか否かを判断し
、排気ガス温度信号に基づきEGR用ソリソレノイドバ
ルブ30二次エア用ソレノイドバルブ44を各々デユー
ティ制御し、圧力センサ56からの排気ガス圧力信号に
基づきバーナー22の燃焼を制御する。そして、このコ
ントロールユニット60は、排気ガスの温度が所定値以
上に高くなり且っ空燃比が所定以上リッチになると触媒
保護手段としての二次エア供給装置46を作動させる制
御手段を構成している。
Further, in FIG. 1, 50 is a cooling water temperature sensor that detects the engine cooling water temperature, 51 is an intake air temperature sensor that detects the engine intake air temperature, 52 is an intake pressure sensor that detects the engine intake pressure, and 54 is NOx Exhaust gas temperature sensor 55 that detects the temperature of exhaust gas upstream of the purification catalyst 22
02 sensor is an air-fuel ratio detection means for detecting the air-fuel ratio of exhaust gas flowing into the NOx purification catalyst, and 56 is a pressure sensor for detecting the pressure of the exhaust gas. It can detect when there is too much adhesion and the filter is clogged. In FIG. 1, 60 is a control unit with a built-in CPU, which receives an engine cooling water temperature signal from the cooling water temperature sensor 50, an engine intake air temperature signal from the intake air temperature sensor 51, and an engine intake air temperature signal from the intake pressure sensor 52. Barometric pressure signal, exhaust gas temperature signal from the exhaust gas temperature sensor 54, exhaust gas air-fuel ratio signal from the 02 sensor 55, exhaust gas pressure signal from the pressure sensor 56, engine speed signal and engine load signal from the fuel injection pump 15. etc., it is determined whether or not to operate the EGR device 232 based on the engine rotation speed signal and the engine load signal, and duty control is performed on the EGR solenoid valve 30 and the secondary air solenoid valve 44 based on the exhaust gas temperature signal. Then, combustion in the burner 22 is controlled based on the exhaust gas pressure signal from the pressure sensor 56. The control unit 60 constitutes a control means that operates the secondary air supply device 46 as a catalyst protection means when the temperature of the exhaust gas becomes higher than a predetermined value and the air-fuel ratio becomes richer than a predetermined value. .

次に、第3図のフローチャートに基づき、二次エア調整
バルブ40に対するデユーティ制御について説明する。
Next, duty control for the secondary air adjustment valve 40 will be explained based on the flowchart in FIG.

まず、ステップSAIで、二次エア用ソレノイドバルブ
44の開閉デユーティ値MAを0に設定して二次エア調
整バルブ40を全閉状態にすると共に、ステップSA2
で、○ニセンサ55により排気ガス中の酸素濃度を検出
して、空燃比(A/F)を計測する。
First, in step SAI, the opening/closing duty value MA of the secondary air solenoid valve 44 is set to 0 to fully close the secondary air adjustment valve 40, and in step SA2
Then, the O sensor 55 detects the oxygen concentration in the exhaust gas and measures the air-fuel ratio (A/F).

ステップSA3で空燃比がリッチか否かを判断し、リッ
チでない場合には、NOx浄化触媒20が劣化するおそ
れがないためステップSAIへ戻り、リッチの場合には
、ステップSA4で排気ガス温度センサ54により排気
ガス温度T1を検出する。
In step SA3, it is determined whether the air-fuel ratio is rich or not. If it is not rich, the process returns to step SAI since there is no risk of deterioration of the NOx purification catalyst 20. If it is rich, the exhaust gas temperature sensor 54 The exhaust gas temperature T1 is detected.

次に、ステップSA5で、排気ガス温度T1と、NOx
浄化触媒20が劣化する領域の下限の温度として設定さ
れた設定排気ガス2!i度T、とを比較して’r+ <
T2か否かを判断し、T、<T、の場合には、NOx浄
化触媒20が劣化するおそれがないため、ステップSA
6で、二次エア用ソレノイドバルブ44の開閉デユーテ
ィ(11i M Aをそのままにしておく。
Next, in step SA5, the exhaust gas temperature T1 and the NOx
Set exhaust gas 2 set as the lower limit temperature of the region where the purification catalyst 20 deteriorates! i degrees T, compared with 'r+ <
It is determined whether T2 or not, and if T<T, there is no risk of deterioration of the NOx purification catalyst 20, so step SA is performed.
6, the opening/closing duty (11i MA) of the secondary air solenoid valve 44 is left as is.

一方、ステップSA5でT1≧T2の場合には、NOx
浄化触媒20が劣化するのを防止するため、ステップS
A7で二次エア用ソレノイドバルブ44の開閉デユーテ
ィ値MAとしてMA+Ml)  ((!!し、MDニ一
定デ二−テイ値)を入れ、排気ガスの空燃比をリーン傾
向にする。
On the other hand, if T1≧T2 in step SA5, NOx
In order to prevent the purification catalyst 20 from deteriorating, step S
At A7, input MA+Ml) ((!!, MD constant duty value) as the opening/closing duty value MA of the secondary air solenoid valve 44 to make the air-fuel ratio of the exhaust gas lean.

このようにして、排気ガスの空燃比がリッチで温度が高
いときに、NOx浄化触媒20の上流側に二次エアが供
給されるので、排気ガスの空燃比がリーン傾向になると
共に排気ガスの温度が低下する。
In this way, when the air-fuel ratio of the exhaust gas is rich and the temperature is high, secondary air is supplied to the upstream side of the NOx purification catalyst 20, so the air-fuel ratio of the exhaust gas tends to be lean and the exhaust gas Temperature decreases.

第4図は本発明の第2実施例に係るディーゼルエンジン
の排気ガス浄化装置を示し、本第2実施例においては、
EGR装r1t32及び二次エア供給装置46が配設さ
れていない代わりに、排気ガスをNOx浄化触媒20の
外周側へバイパスさせる排気ガスバイパス路62と、N
Ox浄化触媒20の上流に配設され、NOx浄化触媒2
0の流入口の開放及び閉塞を行なうバイパスバルブ64
とを備えており、これら排気ガスバイパス路62及びバ
イパスバルブ64とによって、NOx浄化触媒22の劣
化を防止する触媒保護手段66が構成されている。
FIG. 4 shows an exhaust gas purification device for a diesel engine according to a second embodiment of the present invention.
Instead of the EGR system r1t32 and the secondary air supply device 46 being provided, an exhaust gas bypass passage 62 that bypasses the exhaust gas to the outer peripheral side of the NOx purification catalyst 20, and an N
Disposed upstream of the Ox purification catalyst 20, the NOx purification catalyst 2
Bypass valve 64 for opening and closing the inlet of 0
The exhaust gas bypass passage 62 and the bypass valve 64 constitute a catalyst protection means 66 that prevents the NOx purification catalyst 22 from deteriorating.

この第2実施例においては、NOx浄化触媒20が劣化
する条件、つまり排気ガスの空燃比がリッチで且つ温度
が高いときに、バイパスバルブ64を閉塞状態にして、
排気ガスを排気ガスバイパス路62から放出させる。こ
のようにすると、NOx浄化触媒20を劣化させる条件
下にある排気ガスがNOx浄化触媒20を流通しないの
で、NOx浄化触媒20の劣化が防止される。
In this second embodiment, under conditions where the NOx purification catalyst 20 deteriorates, that is, when the air-fuel ratio of the exhaust gas is rich and the temperature is high, the bypass valve 64 is closed.
Exhaust gas is released from the exhaust gas bypass passage 62. In this way, exhaust gas under conditions that degrade the NOx purification catalyst 20 does not flow through the NOx purification catalyst 20, so deterioration of the NOx purification catalyst 20 is prevented.

前記のように、NOx浄化触媒20の外周側に排気ガス
バイパス路62を設けると、排気ガスのバイパス時にN
Ox浄化触媒20の急激な温度低下を防止でき、排気ガ
スがNOx浄化触媒20を流通するよう復帰した際の浄
化性能の低下を防止できる。
As described above, when the exhaust gas bypass path 62 is provided on the outer peripheral side of the NOx purification catalyst 20, when the exhaust gas is bypassed, N
A rapid temperature drop of the Ox purification catalyst 20 can be prevented, and a deterioration in purification performance when the exhaust gas returns to flow through the NOx purification catalyst 20 can be prevented.

また、本第2実施例においては、コントロールユニット
60は、排気ガス温度センサ54からの排気ガス温度信
号、エンジンの回転数、エンジンの負荷及び燃料噴射量
等の信号による、空燃比(A/F)がリッチ運転領域で
あるか否かの判定により、バイパスバルブ64からのバ
イパスバルブポジション信号等を受けてバイパスバルブ
64の開閉を制御する。
In addition, in the second embodiment, the control unit 60 controls the air-fuel ratio (A/F ) is in the rich operating region, the opening/closing of the bypass valve 64 is controlled in response to a bypass valve position signal etc. from the bypass valve 64.

なお、バイパスバルブ64に対する制御としては、全開
と全閉との2fJI類の制御をしてもよいし、NOx浄
化触媒20を劣化させる条件に応じてバイパスバルブ6
4の開度を調節するよう制御してもよい。
Note that the control for the bypass valve 64 may be 2fJI type control of fully open and fully closed, or the bypass valve 64 may be controlled according to the conditions that cause the NOx purification catalyst 20 to deteriorate.
The opening degree of No. 4 may be controlled to be adjusted.

また、排気ガスバイパス路62の構造としては、前記第
2実施例に代えて、第5図に示すように、排気管18に
おけるNOx浄化触媒20が配設された部位と並列に排
気ガスバイパス路62を設けてもよい。
In addition, as for the structure of the exhaust gas bypass passage 62, instead of the second embodiment, as shown in FIG. 62 may be provided.

(発明の効果) 以上説明したように、請求項(1)の発明に係るディー
ゼルエンジンの排気ガス浄化装置によると、NOx浄化
触媒の上流に排気ガス中の微粒子を捕集する微粒子除去
装置を備えているため、排気ガス中の微粒子によるNO
x浄化触媒の浄化性能の低下が防止される。また、触媒
保護手段と、排気ガスの温度が所定値以上に高くなり且
つ空燃比が所定以上にリッチになると前記触媒保護手段
を作動させる制御手段とを備えているため、前記微粒子
除去手段が微粒子を燃焼させるたりして排気ガスがNO
x浄化触媒を劣化させる雰囲気になっても、触媒保護手
段の作動により、NOx浄化触媒の劣化を確実に防止で
きる。
(Effects of the Invention) As explained above, according to the diesel engine exhaust gas purification device according to the invention of claim (1), the particulate removal device for collecting particulates in the exhaust gas is provided upstream of the NOx purification catalyst. NO due to particulates in the exhaust gas.
x The deterioration of the purification performance of the purification catalyst is prevented. Further, since the particulate removal means includes a catalyst protection means and a control means that operates the catalyst protection means when the temperature of the exhaust gas becomes higher than a predetermined value and the air-fuel ratio becomes richer than a predetermined value, the particulate removal means Exhaust gas is reduced to NO by burning
Even if the atmosphere is such that the NOx purification catalyst deteriorates, the catalyst protection means can reliably prevent deterioration of the NOx purification catalyst.

また、請求項(勢の発明に係るエンジンの排気ガス浄化
装置によると、触媒保護手段をNOx浄化触媒の上流に
二次エアを供給する二次エア供給装置としたため、NO
x浄化触媒上流側の排気ガスの温度が所定値以上に高く
なり且つ空燃比が所定以上リッチになると、NOx浄化
装置の上流に二次エアが供給されるので、NOx浄化触
媒の劣化が防止されると共にNOx浄化触媒の浄化性能
が向上する。
Further, according to the engine exhaust gas purification device according to the claimed invention, since the catalyst protection means is a secondary air supply device that supplies secondary air upstream of the NOx purification catalyst, NOx
x When the temperature of the exhaust gas upstream of the purification catalyst becomes higher than a predetermined value and the air-fuel ratio becomes richer than a predetermined value, secondary air is supplied upstream of the NOx purification device, thereby preventing deterioration of the NOx purification catalyst. At the same time, the purification performance of the NOx purification catalyst is improved.

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

第1図〜第3図は本発明の第1実施例を示し、第1図は
ディーゼルエンジンの排気ガス浄化装置の仝体構成図、
第2図はEGR装置の断面図、第3図は二次エア供給装
置の制御方法を示すフローチャート図、第4図は本発明
の第2実施例に係るディーゼルエンジンの排気ガス浄化
装置の全体構成図、第5図は第2実施例の変形例を示す
全体構成図、第6図はNOx浄化触媒における排気ガス
温度とNOx浄化性能との関係を示す図である。 0・・・ディーゼルエンジン 2・・・吸気管 8・・・排気管 0・・・NOx浄化触媒 1・・・DPF 2・・・バーナー 第 3 図 第4 図 品 第 口
1 to 3 show a first embodiment of the present invention, and FIG. 1 is an overall configuration diagram of an exhaust gas purification device for a diesel engine;
FIG. 2 is a sectional view of the EGR device, FIG. 3 is a flowchart showing a method of controlling the secondary air supply device, and FIG. 4 is the overall configuration of an exhaust gas purification device for a diesel engine according to a second embodiment of the present invention. 5 is an overall configuration diagram showing a modification of the second embodiment, and FIG. 6 is a diagram showing the relationship between exhaust gas temperature and NOx purification performance in the NOx purification catalyst. 0...Diesel engine 2...Intake pipe 8...Exhaust pipe 0...NOx purification catalyst 1...DPF 2...Burner 3 Figure 4 Figure port

Claims (2)

【特許請求の範囲】[Claims] (1)排気系にCuを含有するNO_x浄化触媒を備え
たディーゼルエンジンの排気ガス浄化装置において、前
記NO_x触媒の上流に配設され、排気ガス中の微粒子
を捕集し且つ燃焼させる微粒子除去装置と、前記NO_
x浄化触媒の雰囲気を劣化しない雰囲気にする触媒保護
手段と、前記NO_x浄化触媒上流側の排気ガスの温度
を検出する排気ガス温度センサと、前記NO_x浄化触
媒に流入する排気ガスの空燃比を検出する空燃比検出手
段と、前記排気ガス温度センサ及び空燃比検出手段から
の出力信号を受け、前記排気ガスの温度が所定値以上に
高くなり且つ空燃比が所定以上リッチになると前記触媒
保護手段を作動させる制御手段とを備えたことを特徴と
するディーゼルエンジンの排気ガス浄化装置。
(1) In an exhaust gas purification device for a diesel engine equipped with an NO_x purification catalyst containing Cu in the exhaust system, a particulate removal device is disposed upstream of the NO_x catalyst and collects and burns particulates in the exhaust gas. And said NO_
a catalyst protection means for creating an atmosphere around the x purification catalyst that does not deteriorate; an exhaust gas temperature sensor that detects the temperature of the exhaust gas upstream of the NO_x purification catalyst; and an air-fuel ratio of the exhaust gas flowing into the NO_x purification catalyst. receiving output signals from the exhaust gas temperature sensor and the air-fuel ratio detection means, and when the temperature of the exhaust gas becomes higher than a predetermined value and the air-fuel ratio becomes richer than a predetermined value, the catalyst protection means is activated. 1. An exhaust gas purification device for a diesel engine, comprising a control means for operating the device.
(2)前記触媒保護手段は、前記NO_x浄化触媒の上
流に二次エアを供給する二次エア供給装置である請求項
(1)に記載のディーゼルエンジンの排気ガス浄化装置
(2) The exhaust gas purification device for a diesel engine according to claim (1), wherein the catalyst protection means is a secondary air supply device that supplies secondary air upstream of the NO_x purification catalyst.
JP20914989A 1989-08-12 1989-08-12 Exhaust gas purification device for diesel engine Pending JPH0374513A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20914989A JPH0374513A (en) 1989-08-12 1989-08-12 Exhaust gas purification device for diesel engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20914989A JPH0374513A (en) 1989-08-12 1989-08-12 Exhaust gas purification device for diesel engine

Publications (1)

Publication Number Publication Date
JPH0374513A true JPH0374513A (en) 1991-03-29

Family

ID=16568124

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20914989A Pending JPH0374513A (en) 1989-08-12 1989-08-12 Exhaust gas purification device for diesel engine

Country Status (1)

Country Link
JP (1) JPH0374513A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7249455B2 (en) * 2003-12-23 2007-07-31 Arvin Technologies, Inc. Method and apparatus for regenerating a nitrogen oxides absorber
US7984608B2 (en) 2006-01-31 2011-07-26 Caterpillar Inc. Method and system of directing exhaust gas

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7249455B2 (en) * 2003-12-23 2007-07-31 Arvin Technologies, Inc. Method and apparatus for regenerating a nitrogen oxides absorber
US7984608B2 (en) 2006-01-31 2011-07-26 Caterpillar Inc. Method and system of directing exhaust gas

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