JPH0559245B2 - - Google Patents
Info
- Publication number
- JPH0559245B2 JPH0559245B2 JP59234042A JP23404284A JPH0559245B2 JP H0559245 B2 JPH0559245 B2 JP H0559245B2 JP 59234042 A JP59234042 A JP 59234042A JP 23404284 A JP23404284 A JP 23404284A JP H0559245 B2 JPH0559245 B2 JP H0559245B2
- Authority
- JP
- Japan
- Prior art keywords
- filter
- temperature
- nox
- throttle valve
- exhaust gas
- 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 - Fee Related
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/24—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
- F01N3/28—Construction of catalytic reactors
- F01N3/2882—Catalytic reactors combined or associated with other devices, e.g. exhaust silencers or other exhaust purification devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/023—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion
- F01N3/2006—Periodically heating or cooling catalytic reactors, e.g. at cold starting or overheating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion
- F01N3/2006—Periodically heating or cooling catalytic reactors, e.g. at cold starting or overheating
- F01N3/2013—Periodically heating or cooling catalytic reactors, e.g. at cold starting or overheating using electric or magnetic heating means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B3/00—Engines characterised by air compression and subsequent fuel addition
- F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Exhaust Gas After Treatment (AREA)
- Processes For Solid Components From Exhaust (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明はデイーゼル機関の排気浄化装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to an exhaust gas purification device for a diesel engine.
従来の技術
デイーゼル機関は空気過剰のもとで作動せしめ
られるためにデイーゼル機関の排気ガス中には高
濃度の酸素が存在し、従つてガソリン機関に対し
て使用されている還元触媒或いは三元触媒をもつ
てしてはデイーゼル機関の排気ガス中のNOxを
低減することはできない。従つて従来より排気ガ
ス中のNOxを低減するためには触媒が用いられ
ておらず、排気ガスを最循環したり或いは燃料噴
射時間を調整することによりNOxを低減しよう
としているのが現状である。BACKGROUND TECHNOLOGY Diesel engines are operated with excess air, so there is a high concentration of oxygen in the exhaust gas of diesel engines, and therefore the reduction catalyst or three-way catalyst used for gasoline engines is It is not possible to reduce NOx in the exhaust gas of diesel engines. Therefore, conventionally, catalysts have not been used to reduce NOx in exhaust gas, and the current situation is to try to reduce NOx by recirculating the exhaust gas or adjusting the fuel injection time. .
なお、デイーゼル機関の排気ガス中に含まれる
パテイキユレートをフイルタにより捕獲し、この
フイルタに捕獲されたパテイキユレートを燃焼除
去するために吸気通路に設けた絞り弁を絞るよう
にしたデイーゼル機関が特開昭59−150921号公報
に記載されている。このデイーゼル機関では吸気
通路に設けた絞り弁を絞ることにより排気温度を
上昇させてフイルタに捕獲されたパテイキユレー
トを燃焼せしめるものであり、NOxを除去する
ことはできない。 In addition, a diesel engine was developed in Japanese Patent Application Laid-open No. 1989 (1982) in which the particulate matter contained in the exhaust gas of the diesel engine was captured by a filter, and a throttle valve installed in the intake passage was used to burn and remove the particulate matter captured by the filter. -Described in Publication No. 150921. In this diesel engine, the exhaust gas temperature is increased by throttling a throttle valve provided in the intake passage to burn particulate trapped in the filter, and NOx cannot be removed.
発明が解決しようとする問題点
このように従来のデイーゼル機関においては
NOxを触媒により除去することは行つておらず、
再循環排気ガス等によりNOxを除去するように
してもNOxを十分に除去することはできない。Problems to be solved by the invention As described above, in conventional diesel engines,
NOx is not removed using a catalyst.
Even if NOx is removed using recirculated exhaust gas or the like, NOx cannot be removed sufficiently.
問題点を解決するための手段
上記問題点を解決するために本発明によれば、
機関排気通路内にパテイキユレート捕獲用フイル
タを配置すると共にこのフイルタ上にNOx還元
触媒を担持させ、フイルタにより捕獲されたパテ
イキユレートおよび高沸点HCを還元剤として
NOx還元触媒の触媒作用により排気ガス中の
NOxを還元するようにしている。Means for Solving the Problems According to the present invention, in order to solve the above problems,
A filter for capturing particulate matter is placed in the engine exhaust passage, and a NOx reduction catalyst is supported on this filter, and the particulate matter and high boiling point HC captured by the filter are used as reducing agents.
Due to the catalytic action of the NOx reduction catalyst,
We are trying to reduce NOx.
実施例
第1図を参照すると、1は機関本体、2は吸気
マニホルド、3は吸気マニホルド2の集合部に連
結された吸気ダクト、4は排気マニホルド(図示
せず)に連結された排気ダクト、5は排気ダクト
4の出口に連結された排気ターボチヤージヤ、6
は排気ターボチヤージヤ5の出口に連結された排
気管、7は排気管6に連結された別の排気管を夫
夫示す。排気管6はその内部に主通路8と、主通
路8をバイパスするバイパス通路9とを具備し、
主通路8内には円筒状のフイルタ10が配置され
る。一方、バイパス通路9内には負圧ダイアフラ
ム式アクチユエータ11によつて作動せしめられ
るバイパス弁12が挿入され、このバイパス弁1
2は通常閉弁状態に保持される。従つて排気ガス
は通常矢印Aで示すようにフイルタ10内を通
り、排気管7を経て大気に放出される。アクチユ
エータ11はその内部に負圧室を有し、負圧室内
に負圧が加わつたときにはバイパス弁12を全開
し、負圧室内に大気圧が作用したときにはバイパ
ス弁12を閉鎖する。この負圧室は電子制御ユニ
ツト13の出力信号によつて制御される電磁切換
弁14を介して負圧源又は大気に選択に連結され
る。Embodiment Referring to FIG. 1, 1 is an engine main body, 2 is an intake manifold, 3 is an intake duct connected to a gathering part of the intake manifold 2, 4 is an exhaust duct connected to an exhaust manifold (not shown), 5 is an exhaust turbocharger connected to the outlet of the exhaust duct 4; 6;
7 indicates an exhaust pipe connected to the outlet of the exhaust turbocharger 5, and 7 indicates another exhaust pipe connected to the exhaust pipe 6. The exhaust pipe 6 includes a main passage 8 and a bypass passage 9 that bypasses the main passage 8.
A cylindrical filter 10 is arranged within the main passage 8. On the other hand, a bypass valve 12 is inserted into the bypass passage 9 and is operated by a negative pressure diaphragm actuator 11.
2 is normally kept closed. Therefore, the exhaust gas normally passes through the filter 10 as shown by arrow A and is discharged to the atmosphere via the exhaust pipe 7. The actuator 11 has a negative pressure chamber therein, and fully opens the bypass valve 12 when negative pressure is applied to the negative pressure chamber, and closes the bypass valve 12 when atmospheric pressure acts within the negative pressure chamber. This negative pressure chamber is selectively connected to a negative pressure source or to the atmosphere via an electromagnetic switching valve 14 controlled by an output signal of an electronic control unit 13.
電子制御ユニツト13はデイジタルコンピユー
タからなり、双方向性バス15によつて相互に接
続されたRAM(ランダムアクセスメモリ)16、
ROM(リードオンメモリ)17、CRU(マイクロ
プロセツサ)18、入力ポート19および出力ポ
ート20を具備する。電磁切換弁14は駆動回路
21を介して出力ポート20に接続される。一
方、フイルタ10の入口部には放射状に配列され
た電気ヒータ22が配置され、この電気ヒータ2
2は駆動回路23を介して出力ポート20に接続
される。更に、フイルタ10内にはフイルタ10
の温度を検出する温度センサ24が挿入され、こ
の温度センサ24はAD変換器25を介して入力
ポート19に接続される。 The electronic control unit 13 consists of a digital computer, RAM (Random Access Memory) 16, interconnected by a bidirectional bus 15;
It includes a ROM (read-on memory) 17, a CRU (microprocessor) 18, an input port 19, and an output port 20. The electromagnetic switching valve 14 is connected to the output port 20 via a drive circuit 21. On the other hand, electric heaters 22 arranged radially are arranged at the inlet of the filter 10.
2 is connected to the output port 20 via the drive circuit 23. Furthermore, a filter 10 is included in the filter 10.
A temperature sensor 24 that detects the temperature of is inserted, and this temperature sensor 24 is connected to the input port 19 via an AD converter 25.
一方、吸気ダクト3内には負圧ダイアフラム式
アクチユエータ24によつて開閉制御される絞り
弁25が配置される。アクチユエータ24はダイ
アフラムによつて分離された負圧室と大気圧室と
を有し、負圧室は電磁切換弁26を介して負圧源
又は大気に選択的に連結される。アクチユエータ
24のダイアフラムは制御ロツド27を介して絞
り弁25の弁軸28にリンク連結される。アクチ
ユエータ24の負圧室内に負圧が加わると絞り弁
25は閉弁方向に回動せしめられ、アクチユエー
タ24の負圧室内に大気圧が作用すると絞り弁2
5は開弁方向に回動せしめられる。電磁切換弁2
6は駆動回路29を介して出力ポート20に接続
される。絞り弁25の弁軸28には絞り弁25の
開度を検出する絞り弁開度センサ30が取付けら
れ、この絞り弁開度センサ30はAD変換器31
を介して入力ポート19に接続される。また、機
関負荷を検出する負荷センサ、例えば燃料噴射ポ
ンプのラツク位置を検出する負荷センサ32が
AD変換器33を介して入力ポート19に接続さ
れ、機関回転数に比例してパルスを発生する回転
数センサ33が入力ポート19に接続される。
CPU18内においては回転数センサ33の出力パ
ルスから機関回転数が計算される。 On the other hand, a throttle valve 25 whose opening and closing are controlled by a negative pressure diaphragm actuator 24 is disposed within the intake duct 3 . The actuator 24 has a negative pressure chamber and an atmospheric pressure chamber separated by a diaphragm, and the negative pressure chamber is selectively connected to a negative pressure source or the atmosphere via an electromagnetic switching valve 26. The diaphragm of the actuator 24 is linked via a control rod 27 to the valve stem 28 of the throttle valve 25. When negative pressure is applied to the negative pressure chamber of the actuator 24, the throttle valve 25 is rotated in the valve closing direction, and when atmospheric pressure is applied to the negative pressure chamber of the actuator 24, the throttle valve 25 is rotated.
5 is rotated in the valve opening direction. Solenoid switching valve 2
6 is connected to the output port 20 via a drive circuit 29. A throttle valve opening sensor 30 for detecting the opening of the throttle valve 25 is attached to the valve shaft 28 of the throttle valve 25, and this throttle valve opening sensor 30 is connected to an AD converter 31.
is connected to input port 19 via. In addition, a load sensor that detects the engine load, for example, a load sensor 32 that detects the idle position of the fuel injection pump, is installed.
A rotation speed sensor 33 is connected to the input port 19 via an AD converter 33 and generates a pulse in proportion to the engine rotation speed.
In the CPU 18, the engine rotation speed is calculated from the output pulse of the rotation speed sensor 33.
フイルタ10は三次元網目構造をなすコージラ
イトにγ−アルミナをコーテイングしたものであ
り、排気ガス中のパテイキユレート、高沸点HC
は排気ガスがフイルタ10内を流れる間に網目構
造体により捕獲されて網目構造体内に付着堆積せ
しめられる。なお、このフイルタ10は排圧をさ
ほど高めることなくパテイキユレート、高沸点
HCを捕獲できればよいのでフイルタ10の内部
形状は、ハニカム形状、モノリス形状、ペレツト
形状等どのような形状でもよい。 The filter 10 is made of cordierite with a three-dimensional network structure coated with γ-alumina, and filters particulate matter and high boiling point HC in the exhaust gas.
While the exhaust gas flows through the filter 10, it is captured by the mesh structure and deposited therein. Note that this filter 10 can handle particulate matter, high boiling point, etc. without significantly increasing the exhaust pressure.
Since it is sufficient to capture HC, the internal shape of the filter 10 may be any shape such as a honeycomb shape, a monolith shape, or a pellet shape.
本発明による実施例ではγ−アルミナをコーテ
イングしたコージライトからなる担体上にCo、
Fe、Niから選ばれた少くとも一つの金属と希土
類(La、Th、Ce等)と白金族金属(Pt、Rh、
Ru、Pd、Os、Ir等)の三成分からなる触媒が担
持される。これらの触媒は過剰酸素のもとで
NOxに対して強い還元性を有することが判明し
ているがこの強い還元性は後述するように一定の
温度範囲において発揮される。 In an embodiment according to the present invention, Co is deposited on a support made of cordierite coated with γ-alumina.
At least one metal selected from Fe, Ni, rare earths (La, Th, Ce, etc.) and platinum group metals (Pt, Rh,
A catalyst consisting of three components (Ru, Pd, Os, Ir, etc.) is supported. These catalysts under excess oxygen
It has been found that it has a strong reducing property against NOx, and this strong reducing property is exhibited within a certain temperature range as described below.
次にこのような触媒を担持した担体の製造方法
およびNOxの浄化性能について説明する。 Next, a method for producing a carrier supporting such a catalyst and its NOx purification performance will be explained.
担体としては前述したようにγ−アルミナをコ
ーテイングした三次元網目構造のコージライトを
用いる。 As the carrier, cordierite having a three-dimensional network structure coated with γ-alumina is used as described above.
まず始めに硝酸コバルト、硝酸ランタンの混合
液中に担体を浸漬し、Co、Laを担体上に含浸さ
せる。次いで60℃の温風を所定時間吹き当てて乾
燥させる。 First, a carrier is immersed in a mixed solution of cobalt nitrate and lanthanum nitrate to impregnate Co and La onto the carrier. Then, it is dried by blowing warm air at 60°C for a predetermined period of time.
次いでPtの酸性硝酸溶液中に担体を浸漬して
Ptを担体上に吸着させる。次いで60℃の温風を
所定時間吹き当てて乾燥させる。 Then, the support was immersed in an acidic nitric acid solution of Pt.
Adsorb Pt onto a carrier. Then, it is dried by blowing warm air at 60°C for a predetermined period of time.
次いで担体を10%アンモニア水溶液の20℃飽和
蒸気中に10分間さらした後、400℃の水素雰囲気
中に40分間さらしてH2還元を行ない、担体上に
単体のCoを形成する。 Next, the carrier is exposed to saturated steam of a 10% ammonia aqueous solution at 20°C for 10 minutes, and then to a hydrogen atmosphere at 400°C for 40 minutes to perform H 2 reduction and form simple Co on the carrier.
なお、NOxの還元触媒としてはまず始めにCo
とLaを担体上に最初に担持させ、次いでPtを担
体上に担持せしめるのが好ましいことが判明して
いる。 In addition, as a NOx reduction catalyst, Co
It has been found that it is preferable to first deposit Pt and La on the carrier, and then deposit Pt on the carrier.
第4図は斯くして得られた担体を排気通路内に
配置してNOxの浄化性能を試験した結果を示し
ている。この担体は容積が約2000cm2で約360gの
アルミナをコーテイングしてあり、Co、La、Pt
の量は夫々約8.8g、4.0g、1.2gである。第4図
において破線は機関回転数が2000r.p.mのときを
示しており、実線は機関回転数が3000r.p.mのと
きを示している。また第4図において縦軸Cは
NOxの浄化率を示しており、横軸Tは担体の温
度を示している。第4図から担体の温度が350℃
付近においてNOxの浄化率がピークになること
がわかる。なお、第4図においてTの区間、即ち
担体の温度が約300℃から400℃の間においてかな
り浄化率が高く、この温度範囲Tに担体の温度を
維持しておけば高いNOx浄化率が得られること
がわかる。 FIG. 4 shows the results of testing the NOx purification performance of the carrier thus obtained by placing it in an exhaust passage. This carrier has a volume of approximately 2000 cm 2 and is coated with approximately 360 g of alumina, including Co, La, and Pt.
The amounts are approximately 8.8g, 4.0g, and 1.2g, respectively. In FIG. 4, the broken line shows when the engine speed is 2000 rpm, and the solid line shows when the engine speed is 3000 rpm. Also, in Figure 4, the vertical axis C is
It shows the purification rate of NOx, and the horizontal axis T shows the temperature of the carrier. From Figure 4, the temperature of the carrier is 350℃.
It can be seen that the NOx purification rate peaks in the vicinity. In addition, in Fig. 4, the purification rate is quite high in the section T, that is, the temperature of the carrier is between approximately 300°C and 400°C, and if the temperature of the carrier is maintained within this temperature range T, a high NOx purification rate can be obtained. I know that it will happen.
前述したように第1図に示すバイパス弁12は
通常閉弁せしめられており、従つて通常排気ガス
はフイルタ10および主通路8を通つて外気中に
排出される。フイルタ10はγ−アルミナをコー
テイングした三次元網目構造のコージライトを担
体としその上にCo、Fe、Niから選ばれた少くと
も一つの金属と希土類元素と白金族金属の三成分
からなる触媒を担持したものからなる。従つてこ
のフイルタ10を用いて高いNOxの浄化効率を
得るにはフイルタ10を300℃から400℃の間、好
ましくは350℃程度に維持することが必要となる。 As mentioned above, the bypass valve 12 shown in FIG. 1 is normally closed, so that the exhaust gas is normally discharged through the filter 10 and the main passage 8 to the outside air. The filter 10 has a three-dimensional network structure cordierite coated with γ-alumina as a carrier, and a catalyst consisting of at least one metal selected from Co, Fe, and Ni, a rare earth element, and a platinum group metal on the carrier. It consists of what it carries. Therefore, in order to obtain high NOx purification efficiency using this filter 10, it is necessary to maintain the filter 10 at a temperature between 300°C and 400°C, preferably at about 350°C.
次に第2図に示すフローチヤートを参照してフ
イルタ10を350℃程度に維持する方法について
説明する。第2図を参照するとまず始めにステツ
プ40において温度センサ24の出力信号からフ
イルタ10の温度tを検出する。次いでステツプ
41においてフイルタ温tが一定時間低温状態下
にあるとセツトされるフラグがセツトされている
か否かが判別される。通常このフラグはリセツト
されており、従つてステツプ42に進む。ステツプ
42ではフイルタ温tが340℃以下であるか否かが
判別され、t<340℃であればステツプ43に進む。
ステツプ43ではタイマがセツトされているか否か
が判別され、タイマがセツトされていなければス
テツプ44においてタイマをセツトする。このタイ
マは一定時間経過するとリセツトされる。次いで
ステツプ45ではタイマにより定められた一定時
間経過したか否かが判別される。この時間は例え
ば30秒である。一定時間経過していないときには
ステツプ46に進んで絞り弁25の絞り制御が行な
われる。 Next, a method for maintaining the filter 10 at about 350° C. will be explained with reference to the flowchart shown in FIG. Referring to FIG. 2, first, in step 40, the temperature t of the filter 10 is detected from the output signal of the temperature sensor 24. Next, in step 41, it is determined whether a flag that is set when the filter temperature t remains low for a certain period of time is set. Normally this flag will have been reset, so proceed to step 42. step
At step 42, it is determined whether the filter temperature t is below 340°C, and if t<340°C, the process proceeds to step 43.
In step 43, it is determined whether or not the timer has been set. If the timer has not been set, the timer is set in step 44. This timer is reset after a certain period of time has elapsed. Next, in step 45, it is determined whether a certain period of time set by a timer has elapsed. This time is, for example, 30 seconds. If the predetermined period of time has not elapsed, the process advances to step 46 and throttle control of the throttle valve 25 is performed.
絞り弁25を絞ると機関シリンダ内に供給され
る過剰な空気量が減少し、その結果排気ガスの温
度が上昇する。しかしながら絞り弁25を絞りす
ぎると燃焼が悪化する。どの程度絞ると燃焼が悪
化するかはわかつており、従つて燃焼が悪化しな
い範囲で最も排気ガス温が高くなるかもはじめか
らわかつている。燃焼が悪化しない範囲で最も排
気ガス温が高くなる絞り弁25の開度と、機関回
転数および機関負荷との関係は予めROM17内
に記憶されており、ステツプ46ではこの関係に従
つて絞り弁25の開度が制御される。即ち、機関
回転数および負荷によつて定まる絞り弁開度より
も大きくなれば電磁切換弁26を切替えてアクチ
ユエータ24の負圧室を負圧源に連通させること
により絞り弁25の開度を小さくし、機関回転数
および負荷によつて定まる絞り弁開度よりも小さ
くなれば電磁切換弁26を切替えてアクチユエー
タ24の負圧室を大気に開放することにより絞り
弁25の開度を大きくする。このようにして絞り
弁25の開度が機関回転数および機関負荷により
定まる一定開度に保持され、斯くして排気ガス温
が上昇せしめられる。 Throttling the throttle valve 25 reduces the amount of excess air supplied into the engine cylinder, resulting in an increase in the temperature of the exhaust gas. However, if the throttle valve 25 is throttled too much, combustion will deteriorate. It is known from the beginning to what extent the exhaust gas temperature will be the highest within the range without deteriorating combustion. The relationship between the opening degree of the throttle valve 25 at which the exhaust gas temperature is highest within the range that does not deteriorate combustion, the engine speed, and the engine load is stored in advance in the ROM 17, and in step 46, the throttle valve is opened according to this relationship. The opening degree of 25 is controlled. That is, if the opening of the throttle valve becomes larger than the opening of the throttle valve determined by the engine speed and load, the opening of the throttle valve 25 is reduced by switching the electromagnetic switching valve 26 and communicating the negative pressure chamber of the actuator 24 with the negative pressure source. However, if the opening degree of the throttle valve becomes smaller than the opening degree determined by the engine speed and load, the opening degree of the throttle valve 25 is increased by switching the electromagnetic switching valve 26 and opening the negative pressure chamber of the actuator 24 to the atmosphere. In this way, the opening degree of the throttle valve 25 is maintained at a constant opening degree determined by the engine speed and engine load, and thus the exhaust gas temperature is raised.
次いでフイルタ10の温度tが340℃よりも高
くなればステツプ47に進んでフイルタ温tが360
℃よりも高いか否かが判別され、t≦360℃であ
ればそのまま絞り制御が続行される。t>360℃
になればステツプ48に進んで絞り弁制御が停止さ
れ、絞り弁25は全開状態に保持される。従つて
フイルタ10は340℃から360℃の範囲に維持され
るので排気ガス中のNOxが良好に浄化されるこ
とになる。 Next, when the temperature t of the filter 10 becomes higher than 340°C, the process proceeds to step 47 and the filter temperature t becomes 360°C.
It is determined whether or not the temperature is higher than 0.degree. C., and if t≦360.degree. C., the aperture control is continued. t>360℃
If so, the flow advances to step 48, where the throttle valve control is stopped, and the throttle valve 25 is maintained in the fully open state. Therefore, since the temperature of the filter 10 is maintained within the range of 340°C to 360°C, NOx in the exhaust gas is effectively purified.
一方、ステツプ45において一定時間経過した場
合、即ちt<340℃の状態が一定時間経過すると
ステツプ49に進んでフラグがセツトされる。従つ
て以後はステツプ41からステツプ50に進む。ステ
ツプ50ではフイルタ10の温度tが340℃よりも
小さいか否かが判別され、t<340℃の場合には
ステツプ51において電気ヒータ22が作動せしめ
られる。次いでステツプ46に進む。t≧340℃に
なるとステツプ52に進んでフイルタ温tが360℃
よりも小さいか否かが判別され、t≦360℃であ
ればステツプ51に進んでヒータ22が作動し続け
られる。次いでステツプ46に進む。従つてヒータ
22が作動せしめられている間、絞り制御も行な
われていることがわかる。t>360℃になるとス
テツプ53においてヒータ22の作動が停止せしめ
られ、次いでステツプ54においてフラグがリセツ
トされるために再び絞り弁25による絞り制御の
みが続行して行なわれる。 On the other hand, if a certain period of time has elapsed in step 45, that is, if the condition t<340° C. has elapsed for a certain period of time, the process proceeds to step 49 and a flag is set. Therefore, the process proceeds from step 41 to step 50. In step 50, it is determined whether the temperature t of the filter 10 is smaller than 340°C, and if t<340°C, the electric heater 22 is activated in step 51. Then proceed to step 46. When t≧340℃, proceed to step 52 and filter temperature t becomes 360℃.
If t≦360°C, the process advances to step 51 and the heater 22 continues to operate. Then proceed to step 46. Therefore, it can be seen that the aperture control is also being performed while the heater 22 is being operated. When t>360°C, the operation of the heater 22 is stopped in step 53, and the flag is then reset in step 54, so that only the throttle control by the throttle valve 25 continues to be performed again.
このように本発明による実施例では絞り制御の
みによつてフイルタ温tを340℃から360℃の範囲
に維持できれば絞り制御のみによつてフイルタ温
tを制御し、絞り制御のみによつてフイルタ温t
を340℃以上に維持できないときはヒータ制御も
同時に行なうようにしている。従つて前者の場合
には絞り制御が触媒昇温手段を構成し、後者の場
合には絞り制御およびヒータ制御が触媒昇温手段
を構成する。 As described above, in the embodiment according to the present invention, if the filter temperature t can be maintained within the range of 340°C to 360°C only by the aperture control, the filter temperature t is controlled only by the aperture control; t
If it is not possible to maintain the temperature above 340°C, heater control is also performed at the same time. Therefore, in the former case, the throttle control constitutes the catalyst temperature raising means, and in the latter case, the throttle control and the heater control constitute the catalyst temperature raising means.
また、フイルタ10の網目構造体内にはパテイ
キユレート、高沸点HCが捕獲される。フイルタ
10が再生時期になつたら、即ち機関回転数の積
算値が一定値以上になつたら(この場合には不揮
発性のRAMを設ける)又はフイルタ10の上流
の背圧が一定値以上になつたら(この場合には排
気管6内に圧力センサを取付ける)電磁切換弁1
4が作動せしめられてバイパス弁12が開弁せし
められ、次いでヒータ22が作動せしめられてフ
イルタ10に堆積したパテイキユレート、高沸点
HCが燃焼せしめられる。このような再生処理は
公知であるのでここでは詳述しない。しかしなが
ら第1図に示す実施例はパテイキユレート捕獲用
のフイルタ10をNOxの還元用として共用した
ところに一つの特徴がある。この場合、フイルタ
10に捕獲されたパテイキユレート、高沸点HC
がNOxの還元剤として作用するので特に有効で
ある。 Furthermore, particulate and high boiling point HC are captured within the mesh structure of the filter 10. When it is time for the filter 10 to regenerate, that is, when the integrated value of the engine speed exceeds a certain value (in this case, a non-volatile RAM is provided), or when the back pressure upstream of the filter 10 exceeds a certain value (In this case, install a pressure sensor inside the exhaust pipe 6) Solenoid switching valve 1
4 is activated to open the bypass valve 12, and then the heater 22 is activated to remove the particulate and high boiling point deposits on the filter 10.
HC is burned. Since such regeneration processing is well known, it will not be described in detail here. However, the embodiment shown in FIG. 1 has one feature in that the filter 10 for capturing particulate matter is also used for reducing NOx. In this case, the particulate hydrate captured in the filter 10, the high boiling point HC
is particularly effective because it acts as a NOx reducing agent.
第3図に別の実施例を示す。この実施例では排
気管4にモノリス触媒60を内蔵した触媒コンバ
ータ61が連結される。このモノリス触媒60は
第1図に示すフイルタ10と同様にγ−アルミナ
をコーテイングしたコージライトを担体とし、こ
の担体上にCo、Fe、Niから選ばれた少くとも一
つの金属と希土類金属と白金族金属とを担持させ
たものである。ただ、モノリス触媒60は排気ガ
スの流れ方向にまつすぐに延びる多数の孔が穿設
されているのでパテイキユレートを捕獲する能力
はあまりない。この実施例においても絞り弁25
とヒータ22は第1図の実施例と同様に制御され
る。 Another embodiment is shown in FIG. In this embodiment, a catalytic converter 61 having a built-in monolithic catalyst 60 is connected to the exhaust pipe 4. This monolithic catalyst 60 uses cordierite coated with γ-alumina as a carrier, similar to the filter 10 shown in FIG. Group metals are supported. However, since the monolithic catalyst 60 has a large number of holes extending straight in the direction of flow of exhaust gas, it does not have much ability to capture particulate matter. Also in this embodiment, the throttle valve 25
and heater 22 are controlled in the same manner as in the embodiment of FIG.
なお、車両走行中に絞り弁25を絞ると前述し
たように排気ガス温が上昇するが同時に排気ガス
中のNOxの還元剤として作用するHC、CO、パ
テイキユレートおよびパテイキユレート中の
SOF(液状ハイドロカーボン)が増大し、これら
によつてもNOxの浄化を促進することができる。
なお、燃料噴射時期を遅らせると後燃えを生ずる
ために排気ガス温が上昇し、上述の排気ガス中の
還元剤の量も増大するので絞り制御、ヒータ制御
に加えて更に燃料噴射時期を制御することもでき
る。 Note that when the throttle valve 25 is throttled while the vehicle is running, the exhaust gas temperature rises as described above, but at the same time, HC, CO, particulate, and particulate that act as reducing agents for NOx in the exhaust gas are reduced.
SOF (liquid hydrocarbon) increases, and these can also promote NOx purification.
Note that if the fuel injection timing is delayed, afterburning occurs and the exhaust gas temperature rises, and the amount of reducing agent in the exhaust gas mentioned above also increases, so in addition to throttle control and heater control, the fuel injection timing is further controlled. You can also do that.
発明の効果
フイルタにより捕獲されたパテイキユレートお
よび高沸点HCを還元剤としてフイルタに担持さ
れたNOx還元触媒の触媒作用により排気ガス中
に含まれるNOxを良好に還元することができる。Effects of the Invention NOx contained in exhaust gas can be effectively reduced by the catalytic action of the NOx reduction catalyst supported on the filter using particulate and high boiling point HC captured by the filter as reducing agents.
第1図はデイーゼル機関の全体図、第2図はフ
ローチヤート、第3図はデイーゼル機関の別の実
施例を示す全体図、第4図は担体温度とNOxの
浄化率との関係を示す図である。
1……機関本体、3……吸気ダクト、4,6,
7……排気管、8……主通路、9……バイパス通
路、10……フイルタ、12……バイパス弁、1
3……電子制御ユニツト、22……電気ヒータ、
25……絞り弁。
Fig. 1 is an overall diagram of a diesel engine, Fig. 2 is a flowchart, Fig. 3 is an overall diagram showing another embodiment of the diesel engine, and Fig. 4 is a diagram showing the relationship between carrier temperature and NOx purification rate. It is. 1... Engine body, 3... Intake duct, 4, 6,
7...Exhaust pipe, 8...Main passage, 9...Bypass passage, 10...Filter, 12...Bypass valve, 1
3...Electronic control unit, 22...Electric heater,
25... Throttle valve.
Claims (1)
イルタを配置すると共に該フイルタ上にNOx還
元触媒を担持させ、該フイルタにより捕獲された
パテイキユレートおよび高沸点HCを還元剤とし
て該NOx還元触媒の触媒作用により排気ガス中
のNOxを還元するようにしたデイーゼル機関の
排気浄化装置。1. A filter for capturing particulate matter is placed in the engine exhaust passage, and a NOx reduction catalyst is supported on the filter, and the particulate matter and high boiling point HC captured by the filter are used as reducing agents to reduce exhaust gas by the catalytic action of the NOx reduction catalyst. A diesel engine exhaust purification device designed to reduce NOx inside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59234042A JPS61112715A (en) | 1984-11-08 | 1984-11-08 | Exhaust purifying apparatus for diesel engine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59234042A JPS61112715A (en) | 1984-11-08 | 1984-11-08 | Exhaust purifying apparatus for diesel engine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61112715A JPS61112715A (en) | 1986-05-30 |
| JPH0559245B2 true JPH0559245B2 (en) | 1993-08-30 |
Family
ID=16964656
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59234042A Granted JPS61112715A (en) | 1984-11-08 | 1984-11-08 | Exhaust purifying apparatus for diesel engine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61112715A (en) |
Families Citing this family (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0621539B2 (en) * | 1986-12-04 | 1994-03-23 | キヤタラ−工業株式会社 | Patty unit for burning catalyst filter |
| JPH067920B2 (en) * | 1987-03-31 | 1994-02-02 | 株式会社リケン | Exhaust gas purification material and exhaust gas purification method |
| JP2830464B2 (en) * | 1989-12-06 | 1998-12-02 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| JP2501887Y2 (en) * | 1989-12-27 | 1996-06-19 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| JP2591260B2 (en) * | 1990-06-13 | 1997-03-19 | 日産自動車株式会社 | Engine exhaust purification device |
| JP2552430Y2 (en) * | 1990-12-17 | 1997-10-29 | 日産ディーゼル工業株式会社 | Particulate catalyst activation device |
| JP2663720B2 (en) * | 1990-12-26 | 1997-10-15 | トヨタ自動車株式会社 | Diesel engine exhaust purification system |
| CA2097609C (en) * | 1991-10-03 | 1999-03-16 | Shinichi Takeshima | Device for purifying exhaust of internal combustion engine |
| EP0597106B1 (en) * | 1991-10-14 | 1997-04-02 | Toyota Jidosha Kabushiki Kaisha | Exhaust and purification device for internal combustion engines |
| JP2783074B2 (en) * | 1991-10-29 | 1998-08-06 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| WO1993025805A1 (en) * | 1992-06-12 | 1993-12-23 | Toyota Jidosha Kabushiki Kaisha | Exhaust emission control system for internal combustion engine |
| JP3246086B2 (en) * | 1993-06-11 | 2002-01-15 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| US6161378A (en) | 1996-06-10 | 2000-12-19 | Hitachi, Ltd. | Exhaust gas purification apparatus of internal combustion engine and catalyst for purifying exhaust gas internal combustion engine |
| JP3965711B2 (en) | 1996-10-25 | 2007-08-29 | 株式会社日立製作所 | Nitrogen oxide purification catalyst and purification method |
| US6182443B1 (en) | 1999-02-09 | 2001-02-06 | Ford Global Technologies, Inc. | Method for converting exhaust gases from a diesel engine using nitrogen oxide absorbent |
| DE19909796A1 (en) * | 1999-03-05 | 2000-09-07 | Bayerische Motoren Werke Ag | Method and device for increasing the exhaust gas temperature |
| DE10001992A1 (en) * | 2000-01-19 | 2001-07-26 | Volkswagen Ag | Method to temporarily increase exhaust gas temperature of internal combustion engine; involves measuring state of electrical or other consumer to raise motor load and controlling fuel injection |
| DE10323245A1 (en) * | 2003-05-22 | 2004-12-09 | Umicore Ag & Co.Kg | Process for cleaning the exhaust gas of a diesel engine using a diesel oxidation catalytic converter |
| JP2017025729A (en) * | 2015-07-17 | 2017-02-02 | 株式会社豊田中央研究所 | Exhaust purification device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54121324A (en) * | 1978-03-15 | 1979-09-20 | Toyota Motor Corp | Catalyst heater |
| DE3107117A1 (en) * | 1981-02-26 | 1982-09-09 | Kali-Chemie Ag, 3000 Hannover | "PROCESS FOR SEPARATING NO (DOWN ARROW) X (DOWN ARROW) GAS" |
-
1984
- 1984-11-08 JP JP59234042A patent/JPS61112715A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61112715A (en) | 1986-05-30 |
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