JPH11166410A - Exhaust emission control device - Google Patents

Exhaust emission control device

Info

Publication number
JPH11166410A
JPH11166410A JP9334037A JP33403797A JPH11166410A JP H11166410 A JPH11166410 A JP H11166410A JP 9334037 A JP9334037 A JP 9334037A JP 33403797 A JP33403797 A JP 33403797A JP H11166410 A JPH11166410 A JP H11166410A
Authority
JP
Japan
Prior art keywords
exhaust gas
reducing agent
pipe
exhaust
supply pipe
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
JP9334037A
Other languages
Japanese (ja)
Inventor
Mitsuru Hosoya
満 細谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hino Motors Ltd
Original Assignee
Hino Motors Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hino Motors Ltd filed Critical Hino Motors Ltd
Priority to JP9334037A priority Critical patent/JPH11166410A/en
Publication of JPH11166410A publication Critical patent/JPH11166410A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Landscapes

  • Exhaust Gas After Treatment (AREA)
  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To uniformly disperse reducing agents in exhaust gas by providing swirl generator for providing a swirl to an exhaust gas flow in an exhaust pipe upstream from a supply pipe in a device having an NOx catalyst in the exhaust pipe and the supply pipe for introducing reducing agents in the upstream thereof. SOLUTION: Exhaust gas from a diesel engine is passed through an exhaust pipe, cleaned by an NOx catalyst and then discharged into the atmosphere from a muffler. At this time, a pump 4 in a reducing agent supply pipe 10 is actuated, and the proper amount of hydrocarbon reducing agents in a reducing agent tank is injected and added from the supply pipe 10 to the downstream side of a swirl generator 9 provided in the exhaust pipe in the upstream position of the NOx catalyst at a proper time. This swirl generator 9 is constructed in such a manner that a plurality of arcwise laminas 22 are extended radially from the vicinity of the center through-hole 21 of a disk 20 in the radial direction of the disk 20. Thus, the reducing agents injected from the tip part of the supply pipe 10 are sprayed in mists by exhaust gas passed through the center through-hole 21, and then uniformly dispersed in the exhaust gas.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明はディーゼルエンジン
からの排ガス中に含まれる窒素酸化物類(NOx)を低
減するためのNOx触媒を用いる排ガス浄化装置に関
し、さらに詳しくは、処理されるべき排ガス流に系外か
ら予め補充添加される炭化水素(HC)系還元剤の導入
方式及び導入装置を改善して、添加される還元剤がNO
x触媒に到達する以前の比較的短い距離の流動中に排ガ
ス流中へ均一に分散分布するようにすることにより、す
なわち還元剤の偏在分布を防止することにより、NOx
触媒における総合的なNOx低減効率を向上させた排ガ
ス浄化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas purifying apparatus using a NOx catalyst for reducing nitrogen oxides (NOx) contained in exhaust gas from a diesel engine, and more particularly, to an exhaust gas stream to be treated. The introduction method and introduction device of the hydrocarbon (HC) -based reducing agent, which is previously replenished and added from outside the system, is improved so that the added reducing agent is NO
x by uniformly distributing and dispersing the exhaust gas stream in a relatively short distance before reaching the x catalyst, i.e. by preventing uneven distribution of the reducing agent.
The present invention relates to an exhaust gas purifying apparatus having improved overall NOx reduction efficiency in a catalyst.

【0002】[0002]

【従来の技術】ディーゼルエンジンの排ガスは、排気マ
ニホルドから排気管で大気中へ排出される前に触媒によ
る浄化処理及びマフラー装置による消音処理を受ける。
ディーゼルエンジン排ガス中に余剰の空気(酸素)と共
に含まれるNOxを低減するための触媒としては、銅−
ゼオライト系(例:Cu−ZSM5)触媒、貴金属−耐
火性金属酸化物系(例:Pt,Pd,Ir,Rh等/ア
ルミナ、チタニア、ジルコニア等の組合せ)触媒等、種
々のものが提案され公知である。これらの触媒は、ペレ
ット化された形、あるいは一般的にはセラミックスまた
は金属製の貫流ハニカム(モノリス)のような担体表面
上にウオッシュコート(浸漬塗布)された形で用いら
れ、車輌のエンジンからマフラーに至る比較的短い距離
及び制限されたスペースにおいて排ガスを処理しうるよ
うにコンパクトな形態ではあるが、排ガスの流通圧力降
下をできる限り少なくする形態である。
2. Description of the Related Art Exhaust gas from a diesel engine is subjected to a purification treatment by a catalyst and a silencing treatment by a muffler device before being discharged into the atmosphere from an exhaust manifold through an exhaust pipe.
As a catalyst for reducing NOx contained together with excess air (oxygen) in diesel engine exhaust gas, copper-
Various catalysts have been proposed and known, such as zeolite-based (eg, Cu-ZSM5) catalysts, noble metal-refractory metal oxide-based (eg, Pt, Pd, Ir, Rh, etc./alumina, titania, zirconia, etc.) catalysts. It is. These catalysts are used in the form of pellets, or in the form of washcoats (dip-coating) on the surface of a carrier, such as a flow-through honeycomb (monolith), generally made of ceramics or metal, and are used in vehicles. This is a compact form so that the exhaust gas can be treated in a relatively short distance to the muffler and in a limited space, but a form in which the flow pressure drop of the exhaust gas is reduced as much as possible.

【0003】[0003]

【発明が解決しようとする課題】本発明者は、ディーゼ
ルエンジン排ガス中に含まれるNOxをNOx触媒を用
いて浄化する場合に触媒の入口以前で排ガスに添加され
る還元剤、例えばディーゼルエンジン燃料の軽油のよう
な炭化水素(HC)、の導入方式の改変によってNOx
触媒のNOx低減効率がどのように影響されるかについ
て広く研究検討した。その結果、排気管中の排ガスの流
動は概して層流状であるため排気管の断面の一局所に還
元剤を導入すると還元剤蒸気は排ガス流中へ均一に分散
分布しない状態でNOx触媒に到達し、NOx触媒がハ
ニカムに担持されている場合にはハニカムの多数の貫流
孔のうちの限られた一部の貫流孔にのみ優先的に入り、
残部の貫流孔に入る還元剤の量が不足する状態が生じ、
結局、ハニカム担体の断面において触媒機能の利用が不
均衡になることを示す実験結果を得た。従ってこの実験
結果は、触媒の入口以前の排ガス流中における還元剤の
分布を均一化して、触媒断面における還元剤の偏在を無
くすことにより、触媒の機能を触媒断面の全体にわたっ
て均等にかつ充分に利用することができ、NOx低減効
率を向上しうると確信するに至った。従って本発明者は
上記の実験結果に基き、還元剤導入位置からNOx触媒
入口までの短い制限された距離において、排ガス中に還
元剤を均一に分散分布させる手段について検討研究を進
め、その結果、本発明を完成した。
SUMMARY OF THE INVENTION The inventor of the present invention has found that when purifying NOx contained in diesel engine exhaust gas using a NOx catalyst, a reducing agent added to the exhaust gas before the entrance of the catalyst, for example, a diesel engine fuel. NOx by modifying the introduction method of hydrocarbons (HC) such as light oil
We have studied extensively how the NOx reduction efficiency of the catalyst is affected. As a result, the flow of the exhaust gas in the exhaust pipe is generally laminar, so that when the reducing agent is introduced at one location in the cross section of the exhaust pipe, the reducing agent vapor reaches the NOx catalyst without being uniformly dispersed and distributed in the exhaust gas flow. and, NO x catalyst enters only preferentially to a portion of the flow-through holes limited ones of a number of throughflow holes of honeycomb if it is supported on the honeycomb,
Insufficient amount of reducing agent entering the remaining through-holes occurs,
In the end, we obtained experimental results showing that the utilization of the catalytic function becomes unbalanced in the cross section of the honeycomb carrier. Therefore, the results of this experiment show that the function of the catalyst is evenly and sufficiently distributed over the entire cross section of the catalyst by making the distribution of the reducing agent uniform in the exhaust gas stream before the entrance of the catalyst and eliminating the uneven distribution of the reducing agent in the cross section of the catalyst. It was convinced that it could be used and that the NOx reduction efficiency could be improved. Therefore, based on the above experimental results, the present inventor has studied and studied means for uniformly dispersing and reducing the reducing agent in the exhaust gas at a short limited distance from the reducing agent introduction position to the NOx catalyst inlet, and as a result, The present invention has been completed.

【0004】[0004]

【課題を解決するための手段】かくして本発明は、ディ
ーゼルエンジン(1)から排ガスを外部へ排出する排気
管(2)中に設けられたNOx触媒(7)及びそのNO
x触媒の上流側の排気管部分(A)内に炭化水素系還元
剤(5)を導入する供給管(10)の先端を臨ましてな
る排ガス浄化装置において、その供給管位置よりも上流
側の排気管部分(A’)内に、排ガス流に対して渦流を
付与する渦流発生装置(9)を設けたことを特徴とする
排ガス浄化装置を提供する(図1参照)。
Thus, the present invention provides a NOx catalyst (7) provided in an exhaust pipe (2) for discharging exhaust gas from a diesel engine (1) to the outside and its NOx catalyst.
In the exhaust gas purifying apparatus, which faces the tip of the supply pipe (10) for introducing the hydrocarbon-based reducing agent (5) into the exhaust pipe portion (A) on the upstream side of the x catalyst, the exhaust pipe is located upstream of the supply pipe. There is provided an exhaust gas purifying apparatus characterized in that a vortex generator (9) for providing a vortex to an exhaust gas flow is provided in an exhaust pipe portion (A ') (see FIG. 1).

【0005】このような渦流発生装置を設けることによ
り、その上流側でほぼ層流状に流動している排ガス流に
旋回流動を励起し、また透孔による絞り流れにより供給
管から供給される還元剤が放射状に噴出し、排ガス流が
撹乱されるようになる。この渦流発生装置の下流側で還
元剤供給管の先端から注入される炭化水素還元剤は気状
となって排ガスの渦流ないしは撹乱流の中で分散され、
排気管の断面全体にわたって万遍なく均一に分散した状
態で下流に配置された触媒の入口へ到達する。従って触
媒がセラミックまたは金属製のハニカム構造基体(モノ
リス)にウオッシュコートされた場合であっても、ハニ
カムの各貫流孔に還元剤が等分(あるいは同量)流入
し、触媒の全体にわたるNOx低減機能の有効利用が可
能となる。もし層流状態の排ガス流中に還元剤が供給管
の先端から注入されたとすれば、供給管の位置からNO
x触媒までの距離が短いので、還元剤の分散が充分に進
行しないままNOx触媒入口に到達し、還元剤が相対的
に多く分配されるハニカム貫流孔と相対的に少なく分配
されるハニカム貫流孔とが生じ(多くの場合はそれによ
って還元剤の過不足が生じると考えられる)、従って相
対的に見て触媒機能の利用が不完全となるものと考えら
れる。
By providing such a vortex generator, a swirling flow is excited in an exhaust gas flow flowing almost laminarly on the upstream side, and a reduction flow supplied from a supply pipe by a throttle flow through a through hole is provided. The agent spouts radially, causing the exhaust gas flow to become disturbed. The hydrocarbon reducing agent injected from the tip of the reducing agent supply pipe downstream of the vortex generator is dispersed in the vortex or turbulent flow of the exhaust gas in a gaseous state,
The catalyst reaches the inlet of the catalyst arranged downstream in a state of being uniformly dispersed throughout the cross section of the exhaust pipe. Therefore, even when the catalyst is wash-coated on a ceramic or metal honeycomb structure base (monolith), the reducing agent flows into each through-hole of the honeycomb equally (or in the same amount) to reduce NOx throughout the catalyst. The function can be used effectively. If the reducing agent is injected into the laminar exhaust gas stream from the end of the supply pipe, NO
Since the distance to the x catalyst is short, the dispersion of the reducing agent does not proceed sufficiently and reaches the NOx catalyst inlet, and the honeycomb through-holes in which the reducing agent is distributed relatively more and the honeycomb through-holes in which the reducing agent is relatively less distributed. (Which in most cases would result in excess or deficiency of the reducing agent), and therefore, the use of the catalytic function is considered to be relatively incomplete.

【0006】本発明の排ガス浄化装置において用いられ
る渦流発生装置は、排気管中に排気管を横切るようにフ
ランジで固定された円板からなり、その円板に例えば切
り込み加工及び折り込み加工からなるプレス加工等で形
成される複数のガス流通孔及びその流通孔に対応する傾
斜起立翼(または葉状片)を有するのが好ましい。これ
らの起立翼(または葉状片)の数、寸法、形状及び傾斜
角度等は、排気管中を流れる排ガスに対して旋回流動モ
ーメントを与え、注入還元剤を良く分散させるのに充分
な撹乱流を発生させ、しかも排ガス流に過度の抵抗を与
えないように設計される。
The eddy current generator used in the exhaust gas purifying apparatus of the present invention comprises a disk fixed by a flange in an exhaust pipe so as to cross the exhaust pipe, and the disk is formed by, for example, cutting and folding. It is preferable to have a plurality of gas flow holes formed by processing or the like and inclined rising wings (or leaf-shaped pieces) corresponding to the gas flow holes. The number, size, shape, inclination angle, etc. of these standing wings (or leaf-shaped pieces) give a swirling flow moment to the exhaust gas flowing in the exhaust pipe, and generate sufficient turbulent flow to disperse the injection reducing agent well. It is designed to generate and not add excessive resistance to the exhaust gas flow.

【0007】好ましい渦流発生装置の一例を図3に平面
図で示す。図示される渦流発生装置(9)は円板(2
0)からなり、中心透孔(21)を有し、その中心透孔
付近から円板の半径方向に放射状に延在する複数の弧状
葉片(22)を、例えば切り込み加工操作及び折り込み
加工操作を含むプレス成形加工によって片面に、例えば
約45°の傾斜角で起立させている。このような渦流発
生装置は図2の部分拡大図に示されるようにフランジに
よって、排気管を横切って設置することができる。弧状
葉片(22)は下流側の面において斜めに起立してお
り、その傾斜角によって排ガス流に旋回流動モーメント
を与える。中心透孔(21)の直ぐ下流の位置に還元剤
供給管(10)の先端部を配置し、そこで注入された還
元剤が中心透孔(21)を通り抜けた排ガスで霧吹き状
態になり、さらに周囲の旋回流中へ急速に取り込まれ、
NOx触媒(7)の入口に到達するまでに均一な分散が
達成される。
FIG. 3 is a plan view showing an example of a preferred vortex generator. The illustrated vortex generator (9) has a circular plate (2).
0), having a central through hole (21), and extending a plurality of arc-shaped leaf pieces (22) radially extending from the vicinity of the central through hole in the radial direction of the disc by, for example, cutting and folding operations. It is erected on one side at an inclination angle of, for example, about 45 ° by press forming including the above. Such a vortex generator can be installed across the exhaust pipe by means of a flange, as shown in the partially enlarged view of FIG. The arc-shaped leaf piece (22) stands obliquely on the downstream surface, and imparts a swirling flow moment to the exhaust gas flow by its inclination angle. The distal end of the reducing agent supply pipe (10) is disposed immediately downstream of the central through-hole (21), where the injected reducing agent is atomized by the exhaust gas passing through the central through-hole (21), and Quickly taken into the surrounding swirling flow,
A uniform dispersion is achieved before reaching the inlet of the NOx catalyst (7).

【0008】なお図3の渦流発生装置(9)は、弧状の
葉片(22)を有しているが、この葉片の形状、寸法、
数、配列(位置、対称または非対称)等は容易に改変し
うるものであり、例えば形状については三角形、矩形、
細長半楕円形、台形等の形状としうる。適度な旋回流動
モーメントを排ガス流に与えるが、過度な流動抵抗を与
えないような設計とすべきである。葉片(22)の起立
面は30〜60°、好ましくは40〜50°付近であ
る。
The vortex generator (9) shown in FIG. 3 has arc-shaped leaf pieces (22).
Numbers, arrangements (positions, symmetrical or asymmetrical), etc. can be easily modified, such as triangular, rectangular,
The shape may be an elongated semi-elliptical shape, a trapezoid, or the like. The design should provide a moderate swirling flow moment to the exhaust gas flow but not excessive flow resistance. The upright surface of the leaf piece (22) is around 30 to 60 °, preferably around 40 to 50 °.

【0009】本発明の排ガス浄化装置をディーゼルエン
ジンに関して使用する場合の概要は図1に示される通り
であって、ディーゼルエンジン(1)からの排ガスはマ
ニホルドを経て排気管(2)内を通り、渦流発生装置
(9)及びNOx触媒(7)で浄化され、最後にマフラ
ー(8)を経て排出される。図示されていないがエンジ
ン(1)には、回転センサ及び負荷センサが付設され、
排気管(2)には温度センサが付設され、これらにセン
サからの出力信号はコンピュータ制御装置(ECU)に
入力され、その結果の制御信号が、還元剤供給管(1
0)中のポンプ(4)を作動させ、還元剤タンク(6)
から適切なタイミングで適切な量の還元剤(5)を、排
気管(2)中の渦流発生装置(9)の下流へ注入添加す
る。還元剤は、通常はディーゼル燃料の軽油であるが、
その他の適当な炭化水素類であってもよい。またアンモ
ニアを還元剤として使用することも可能である。
FIG. 1 shows an outline of the case where the exhaust gas purifying apparatus of the present invention is used for a diesel engine. Exhaust gas from a diesel engine (1) passes through a manifold and passes through an exhaust pipe (2). It is purified by a vortex generator (9) and a NOx catalyst (7), and finally discharged through a muffler (8). Although not shown, the engine (1) is provided with a rotation sensor and a load sensor,
A temperature sensor is attached to the exhaust pipe (2), and an output signal from the sensor is input to a computer control unit (ECU), and a control signal resulting therefrom is sent to the reducing agent supply pipe (1).
Activate pump (4) in 0) and reducer tank (6)
And an appropriate amount of the reducing agent (5) is injected into the exhaust pipe (2) downstream of the vortex generator (9) at an appropriate timing. The reducing agent is usually diesel fuel gas oil,
Other suitable hydrocarbons may be used. Ammonia can also be used as a reducing agent.

【0010】還元剤供給管(10)で排気管(2)中へ
注入された還元剤(例:軽油)は、上流に配置された渦
流発生装置(9)の作用で撹乱された渦流状の排ガス中
へ気状となって均一に分散され、NOx触媒(7)の入
口の断面全体にわたって均等に分配され、多数のハニカ
ム貫流孔を通過しNOx浄化を行なう。従って触媒の機
能が局所的ではなく万遍に利用され、従ってNOx浄化
が効率よく達成される。NOx触媒(7)から流出する
浄化された排ガスは、次いで消音のためマフラー(8)
を経てから、大気中へ放出される。
[0010] The reducing agent (eg, light oil) injected into the exhaust pipe (2) through the reducing agent supply pipe (10) is formed into a vortex flow which is disturbed by the action of a vortex generator (9) arranged upstream. The gaseous gas is uniformly dispersed in the exhaust gas, uniformly distributed over the entire cross section of the inlet of the NOx catalyst (7), and passes through a large number of honeycomb through-holes to purify NOx. Therefore, the function of the catalyst is utilized not locally but uniformly, so that NOx purification is efficiently achieved. The purified exhaust gas flowing out of the NOx catalyst (7) is then muffled (8) for silencing
After that, it is released into the atmosphere.

【0011】さらには、従来、図1の装置において渦流
発生装置を用いずに、供給管(10)の位置で二流体ノ
ズル装置を用いて軽油(還元剤)と圧縮空気(例えばエ
アコンプレッサ供給による圧縮空気の一部)を噴射する
ことも行われてきた。
Further, conventionally, light oil (reducing agent) and compressed air (for example, supplied by an air compressor) are supplied by using a two-fluid nozzle device at the position of the supply pipe (10) without using the vortex generator in the device of FIG. Injection of compressed air).

【0012】しかしこの方法であると、還元剤である軽
油が二流体ノズル装置の先端のところで排ガスの高温度
に直接に曝されて、部分的に炭化し、その炭化物が二流
体ノズル装置の先端部に沈積してノズル細孔を閉塞して
しまう問題が生じることがあった。
However, according to this method, the light oil as the reducing agent is directly exposed to the high temperature of the exhaust gas at the tip of the two-fluid nozzle device, and is partially carbonized, and the carbide is removed at the tip of the two-fluid nozzle device. In some cases, a problem may occur in which the nozzle pores are deposited on the portion and block the nozzle pores.

【0013】ところが図1に示される如き本発明の排ガ
ス浄化装置において二流体ノズル装置を用いて還元剤
(炭化水素)と空気とを同時に噴射する場合に、排気管
(2)に30〜60°の角度で合流するように付設した
枝管(12)内壁に、例えばネジ込みにより、二流体ノ
ズル装置(11)を取り付けることにより(図4参
照)、従来の炭素沈積によるノズルの詰まりの問題が著
しく軽減され、しかも本発明の渦流発生装置の効果と相
俟ってNOx低減効率が向上される。この場合に二流体
ノズル装置(11)のノズル先端部を排気管(2)の排
ガス本流域(13)から引っ込んだ枝管(12)内部分
(14)に配置して、高温の排ガス本流に直接に触れな
いようにすると炭化物沈積の問題はさらに軽減される。
However, in the exhaust gas purifying apparatus of the present invention as shown in FIG. 1, when a reducing agent (hydrocarbon) and air are simultaneously injected by using a two-fluid nozzle device, the exhaust pipe (2) has a temperature of 30 to 60 °. By attaching the two-fluid nozzle device (11) to the inner wall of the branch pipe (12) attached to join at an angle of, for example, by screwing (see FIG. 4), the problem of clogging of the nozzle due to the conventional carbon deposition is solved. This is significantly reduced, and the NOx reduction efficiency is improved in combination with the effect of the eddy current generator of the present invention. In this case, the tip of the nozzle of the two-fluid nozzle device (11) is disposed in the portion (14) of the exhaust pipe (2) inside the branch pipe (12) which is withdrawn from the exhaust gas main stream area (13), so that the hot exhaust gas main stream is formed. Avoiding direct contact further reduces the problem of carbide deposition.

【0014】従って本発明は、ディーゼルエンジン
(1)から排ガスを外部へ排出する排気管(2)中に設
けられたNOx触媒(7)及びそのNOx触媒の上流側
の排気管部分(A)内に炭化水素系還元剤(5)を導入
する供給管(10)の先端を臨ましてなる排ガス浄化装
置において、その供給管位置よりも上流側の排気管部分
(A’)内に、排ガス流に対して旋回流動モーメントを
部分的に付与し、絞り流により還元剤が放射状に噴射す
る渦流発生装置(9)を設け、かつ上記供給管(10)
が還元剤と圧縮空気とを一緒に噴射する二流体ノズル装
置であり、そして排気管(2)に30〜60°の角度で
合流するように付設した枝管(12)内に取り付けられ
ていることを特徴とする排ガス浄化装置を提供する。
Accordingly, the present invention provides a NOx catalyst (7) provided in an exhaust pipe (2) for discharging exhaust gas from a diesel engine (1) to the outside and an exhaust pipe portion (A) upstream of the NOx catalyst. In the exhaust gas purification device facing the end of the supply pipe (10) for introducing the hydrocarbon-based reducing agent (5) into the exhaust pipe section (A ') upstream of the supply pipe position, A swirling flow generating device (9) is provided for partially imparting a swirling flow moment, and a reducing agent is radially injected by a throttle flow, and the supply pipe (10) is provided.
Is a two-fluid nozzle device for injecting the reducing agent and the compressed air together, and is mounted in a branch pipe (12) attached to the exhaust pipe (2) at an angle of 30 to 60 °. An exhaust gas purifying apparatus characterized by the above feature is provided.

【0015】[0015]

【実施例1】触媒の調製 硝酸銀、ゼオライトZSM−5を水に分散させ、さらに
バインダーとしてシリカゾルを加えスラリーとした。こ
れをハニカムにコーティングし、その後乾燥、焼成し
た。これに所定量の硝酸銅水溶液を用い含浸させ、乾燥
した後500℃で1.5時間焼成した。
Example 1 Preparation of Catalyst Silver nitrate and zeolite ZSM-5 were dispersed in water, and silica sol was further added as a binder to form a slurry. This was coated on a honeycomb, and then dried and fired. This was impregnated with a predetermined amount of an aqueous solution of copper nitrate, dried, and fired at 500 ° C. for 1.5 hours.

【0016】試験 このようにして得られた担持NOx触媒を図1に示すよ
うな排ガス浄化装置(I)及びそれから渦流発生装置を
削除した装置(II:比較)にそれぞれ装着した。
Tests The supported NOx catalysts thus obtained were mounted on an exhaust gas purifying device (I) as shown in FIG. 1 and a device (II: comparison) in which the vortex generator was omitted therefrom.

【0017】これらの装置に、ディーゼルエンジン排ガ
スを250℃〜550℃に負荷を変えてコントロール
し、空間速度20,000hr-1で通過させ、還元剤と
して軽油を、軽油/NO=2の重量比で噴射し、NOx
低減率を測定した。結果を図5にグラフで示す。
The exhaust gas of a diesel engine is controlled by changing the load to 250 ° C. to 550 ° C. in these devices, and is passed at a space velocity of 20,000 hr −1 , and light oil is used as a reducing agent in a weight ratio of light oil / NO = 2 Inject with NOx
The reduction rate was measured. The results are shown graphically in FIG.

【0018】[0018]

【実施例2】図1の装置における還元剤供給管(10)
の代りに図4の方式で二流体ノズル(11)を取り付け
た装置I(本発明)と、枝管(12)を設けずに単に供
給管の代わりに二流体ノズルを排気管内に挿入取り付け
た装置II(比較)を用いて、実施例1の実験を繰り返
えした。累計1週間の連続試験においてノズル先端部に
おける炭化物沈積トラブル発生回数は装置Iについては
0回/週、装置IIについては7回/週の割合であっ
た。NOx低減率の結果を図6にグラフで示す。
Embodiment 2 Reducing agent supply pipe (10) in the apparatus of FIG.
Instead of the apparatus I (invention) equipped with a two-fluid nozzle (11) in the manner of FIG. 4, a two-fluid nozzle was inserted and mounted in the exhaust pipe instead of the supply pipe without providing the branch pipe (12). The experiment of Example 1 was repeated using apparatus II (comparative). In the continuous test for a total of one week, the number of occurrences of carbide deposition trouble at the nozzle tip was 0 times / week for the apparatus I and 7 times / week for the apparatus II. FIG. 6 is a graph showing the result of the NOx reduction rate.

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

【図1】本発明の排ガス浄化装置の概略断面図。FIG. 1 is a schematic sectional view of an exhaust gas purifying apparatus of the present invention.

【図2】渦流発生装置の取り付けを示す図1の部分拡大
図。
FIG. 2 is a partially enlarged view of FIG. 1 showing attachment of a vortex generator.

【図3】渦流発生装置の一例の平面図。FIG. 3 is a plan view of an example of a vortex generator.

【図4】二流体ノズルによる還元剤添加方式採用の本発
明装置の一例の断面図。
FIG. 4 is a cross-sectional view of an example of the apparatus of the present invention employing a reducing agent addition method using a two-fluid nozzle.

【図5】実施例1のNOx低減率測定結果を示すグラ
フ。
FIG. 5 is a graph showing a measurement result of a NOx reduction rate in Example 1.

【図6】実施例2のNOx低減率測定結果を示すグラ
フ。
FIG. 6 is a graph showing a measurement result of a NOx reduction rate in Example 2.

【符号の説明】[Explanation of symbols]

1 ディーゼルエンジン 2 排気管 5 還元剤(炭化水素系) 7 NOx触媒 8 マフラー 9 渦流発生装置 10 還元剤供給管 DESCRIPTION OF SYMBOLS 1 Diesel engine 2 Exhaust pipe 5 Reducing agent (hydrocarbon type) 7 NOx catalyst 8 Muffler 9 Eddy current generator 10 Reducing agent supply pipe

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F01N 3/24 B01D 53/34 129E ZAB ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI F01N 3/24 B01D 53/34 129E ZAB

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 ディーゼルエンジンから排ガスを外部へ
排出する排気管(2)中に設けられたNOx触媒(7)
及びそのNOx触媒の上流側の排気管部分(A)内に炭
化水素系還元剤(5)を導入する供給管(10)の先端
を臨ましてなる排ガス浄化装置において、その供給管位
置よりも上流側の排気管部分(A’)内に、排ガス流に
対して渦流を付与する渦流発生装置(9)を設けたこと
を特徴とする上記排ガス浄化装置。
A NOx catalyst (7) provided in an exhaust pipe (2) for discharging exhaust gas from a diesel engine to the outside.
And an exhaust gas purifying apparatus in which an end of a supply pipe (10) for introducing a hydrocarbon-based reducing agent (5) into an exhaust pipe portion (A) on the upstream side of the NOx catalyst faces upstream of the supply pipe. A swirl generator (9) for providing a swirl to the exhaust gas flow in the exhaust pipe portion (A ') on the side of the exhaust gas purifier.
【請求項2】 渦流発生装置(9)が中心透孔(21)
を有する円板(20)からなり、その中心透孔の周縁を
外れた位置から円板の半径方向に放射状に延在する複数
の弧状葉片(22)を片面に傾斜起立させてなる構造で
あり、それらの弧状葉片起立面が下流側に配置されるよ
うに排気管を横切って設けられている請求項1の排ガス
浄化装置。
2. A vortex generator (9) having a central through hole (21).
And a plurality of arc-shaped leaf pieces (22) extending radially in a radial direction of the disc from a position outside the periphery of the center through hole and having a tilted upright standing on one surface. The exhaust gas purifying apparatus according to claim 1, wherein the arc-shaped leaf piece standing surface is provided across the exhaust pipe so as to be disposed on the downstream side.
【請求項3】 炭化水素系還元剤を導入する還元剤供給
管(10)が還元剤と圧縮空気を噴射する二流体ノズル
装置(11)であり、そして排気管(2)に30〜60
°の角度で合流するように付設した枝管(12)内に取
り付けられていることを特徴とする請求項1または2の
排ガス浄化装置。
3. A reducing agent supply pipe (10) for introducing a hydrocarbon-based reducing agent is a two-fluid nozzle device (11) for injecting a reducing agent and compressed air, and an exhaust pipe (2) having 30 to 60 nozzles.
3. The exhaust gas purifying apparatus according to claim 1, wherein the exhaust gas purifying apparatus is mounted in a branch pipe (12) provided so as to merge at an angle of °.
【請求項4】 二流体ノズル装置(11)のノズル先端
部を排気管(2)内の排ガス本流域(13)から引っ込
んだ枝管(12)内部分(14)に配置したことを特徴
とする請求項3のガス浄化装置。
4. The two-fluid nozzle device (11) is characterized in that the tip of the nozzle is disposed in a portion (14) inside a branch pipe (12) which is withdrawn from a main exhaust gas flow area (13) in an exhaust pipe (2). The gas purifying apparatus according to claim 3, wherein
JP9334037A 1997-12-04 1997-12-04 Exhaust emission control device Pending JPH11166410A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9334037A JPH11166410A (en) 1997-12-04 1997-12-04 Exhaust emission control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9334037A JPH11166410A (en) 1997-12-04 1997-12-04 Exhaust emission control device

Publications (1)

Publication Number Publication Date
JPH11166410A true JPH11166410A (en) 1999-06-22

Family

ID=18272806

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9334037A Pending JPH11166410A (en) 1997-12-04 1997-12-04 Exhaust emission control device

Country Status (1)

Country Link
JP (1) JPH11166410A (en)

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