[go: up one dir, main page]

JP6046568B2 - Exhaust purification device - Google Patents

Exhaust purification device Download PDF

Info

Publication number
JP6046568B2
JP6046568B2 JP2013158677A JP2013158677A JP6046568B2 JP 6046568 B2 JP6046568 B2 JP 6046568B2 JP 2013158677 A JP2013158677 A JP 2013158677A JP 2013158677 A JP2013158677 A JP 2013158677A JP 6046568 B2 JP6046568 B2 JP 6046568B2
Authority
JP
Japan
Prior art keywords
exhaust
exhaust gas
flow
wall surface
gap
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.)
Active
Application number
JP2013158677A
Other languages
Japanese (ja)
Other versions
JP2015031158A (en
Inventor
オリビエ フルニエ
オリビエ フルニエ
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.)
Marelli Corp
Original Assignee
Calsonic Kansei 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 Calsonic Kansei Corp filed Critical Calsonic Kansei Corp
Priority to JP2013158677A priority Critical patent/JP6046568B2/en
Priority to CN201420354201.7U priority patent/CN203978582U/en
Publication of JP2015031158A publication Critical patent/JP2015031158A/en
Application granted granted Critical
Publication of JP6046568B2 publication Critical patent/JP6046568B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Exhaust Gas After Treatment (AREA)
  • Processes For Solid Components From Exhaust (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Description

本発明は、内燃機関の排気浄化装置に関し、特に排気通路に配置される撹拌手段に関するものである。   The present invention relates to an exhaust emission control device for an internal combustion engine, and more particularly to a stirring means disposed in an exhaust passage.

従来、内燃機関の排気浄化装置として、特許文献1に示すように、撹拌手段、噴射ノズル、SCR触媒(選択還元型触媒)、および酸化触媒を備えたものがある。この排気浄化装置は、まず撹拌手段によって排気ガスの流れを旋回流に変え、旋回流に添加剤(尿素水溶液)を噴射することで、排気ガスと添加剤を混合する。排気ガスと添加剤を混合することで、添加剤中の尿素が、排気熱、および排気ガス中の水蒸気によって加水分解され、アンモニアが生成される。そして、排気ガス中の窒素酸化物とアンモニアがSCR触媒によって窒素に還元され、余剰アンモニアが酸化触媒によって窒素、および窒素酸化物に酸化される。   2. Description of the Related Art Conventionally, as disclosed in Patent Document 1, an exhaust gas purification apparatus for an internal combustion engine includes an agitation unit, an injection nozzle, an SCR catalyst (selective reduction catalyst), and an oxidation catalyst. In this exhaust purification device, first, the flow of the exhaust gas is changed to a swirling flow by the stirring means, and the additive gas (urea aqueous solution) is injected into the swirling flow, thereby mixing the exhaust gas and the additive. By mixing the exhaust gas and the additive, urea in the additive is hydrolyzed by the exhaust heat and water vapor in the exhaust gas, thereby generating ammonia. Then, nitrogen oxides and ammonia in the exhaust gas are reduced to nitrogen by the SCR catalyst, and surplus ammonia is oxidized to nitrogen and nitrogen oxides by the oxidation catalyst.

特開2009−24628号公報JP 2009-24628 A

ところで、上記のような排気浄化装置は、撹拌手段によって排気ガスの流れを旋回流に変えるように構成されているため、噴射された添加剤が遠心力によって排気管の内壁面に衝突、付着してしまう。そして、付着した添加剤は、結晶化して堆積し、排気系部品を腐食してしまうという課題があった。   By the way, the exhaust purification apparatus as described above is configured to change the flow of the exhaust gas into a swirling flow by the stirring means, so that the injected additive collides with and adheres to the inner wall surface of the exhaust pipe by centrifugal force. End up. Then, the adhering additive is crystallized and deposited, and there is a problem that the exhaust system parts are corroded.

そこで、本発明は、排気管の内壁面に付着する添加剤を低減しつつ、排気ガスと添加剤とを撹拌、混合することができる排気浄化装置を提供することを目的としている。   Therefore, an object of the present invention is to provide an exhaust purification device that can stir and mix the exhaust gas and the additive while reducing the additive adhering to the inner wall surface of the exhaust pipe.

上記の課題を解決するために、本発明は、内燃機関の排気管14内に配置される撹拌手段5を備えた排気浄化装置1であって、撹拌手段5は、排気ガスの流れ方向に沿って配置され、排気ガスの流れを整える板状の整流部51と、該整流部51の下流側に排気ガスを旋回流に変える旋回部53とを有し、前記整流部51は複数の整流片51aで構成され、該整流片51aの前記排気管14の内壁面14aに対向する径方向外側端部と前記内壁面14aとの間に第1の隙間14bが形成され、前記旋回部53は、前記整流片51aの下流側に扇形状に延設された扇形状部を有し、該扇形状部の円弧縁53bは前記内壁面14aに面し、前記円弧縁53bと前記内壁面14aとに間に第2の隙間14cが形成されると共に前記第1の隙間14b及び前記第2の隙間14cは、その径方向寸法が周方向に対して一定に設定され、前記排気管14内を排気ガスが流れる際に、前記第1の隙間14b及び前記第2の隙間14cの下流側に筒状に、排気ガスが該排気管14の中心軸Oの軸方向に沿って流れる直進流路21と、該直進流路21の筒内側に、排気ガスが該中心軸Oの該軸方向に対して旋回しつつ流れる旋回流路22とが形成されることを特徴としている。
In order to solve the above problems, the present invention is an exhaust purification device 1 including a stirring means 5 disposed in an exhaust pipe 14 of an internal combustion engine, and the stirring means 5 is along the flow direction of the exhaust gas. And a plate-like rectifying unit 51 that regulates the flow of exhaust gas, and a swirl unit 53 that converts the exhaust gas into a swirling flow downstream of the rectifying unit 51, and the rectifying unit 51 includes a plurality of rectifying pieces A first gap 14b is formed between the radially outer end of the rectifying piece 51a facing the inner wall surface 14a of the exhaust pipe 14 and the inner wall surface 14a. There is a fan-shaped portion extending in a fan shape on the downstream side of the rectifying piece 51a, and the arc edge 53b of the fan-shaped portion faces the inner wall surface 14a, and the arc edge 53b and the inner wall surface 14a with the second gap 14c is formed between the first clearance 14b Fine said second gap 14c is set to a constant its radial dimension is the circumferential direction, when flowing through the inside of the exhaust pipe 14 is an exhaust gas, said first gap 14b and the second gap 14c A rectilinear flow path 21 in which the exhaust gas flows along the axial direction of the central axis O of the exhaust pipe 14 in a cylindrical shape on the downstream side of the exhaust pipe 14. A swirl flow path 22 that flows while swirling with respect to the axial direction is formed.

本発明は、配管14内で、旋回流は、直進流にぶつかりつつ、旋回を続けるため、添加剤は内壁面14aに付着せずに排気ガス中に撹拌される。これによって、添加剤が均一に分布するとともに、配管14の内壁に付着、堆積する添加剤が減少し、排気系部品における腐食の発生を抑制することができる。   In the present invention, since the swirling flow continues to swirl in the pipe 14 while colliding with the straight flow, the additive is agitated in the exhaust gas without adhering to the inner wall surface 14a. As a result, the additive is uniformly distributed, the additive adhering to and depositing on the inner wall of the pipe 14 is reduced, and the occurrence of corrosion in the exhaust system parts can be suppressed.

本発明の一実施形態を示し、排気浄化装置の全体構成図である。1 is an overall configuration diagram of an exhaust emission control device according to an embodiment of the present invention. 本発明の一実施形態を示し、図1のII-II線に沿った断面図である。FIG. 2 is a cross-sectional view taken along the line II-II in FIG. 1, showing an embodiment of the present invention. 本発明の一実施形態を示し、図2のIII-III線に沿った断面図である。FIG. 3 shows an embodiment of the present invention and is a cross-sectional view taken along the line III-III in FIG. 2. 本実施形態のミキサを示す斜視図である。It is a perspective view which shows the mixer of this embodiment. 本実施形態のミキサを構成する複合構成材を示す平面図で、(a)は下流側、(b)は中央側、(c)は上流側で単位構成材が連結していることを示している。It is a top view which shows the composite structural material which comprises the mixer of this embodiment, (a) shows the downstream, (b) shows the center side, (c) shows that the unit structural material has connected with the upstream. Yes. 第1エルボ部から第2チャンバ部までの配管内の流速を示すベクトル線図である。It is a vector diagram which shows the flow velocity in piping from a 1st elbow part to a 2nd chamber part. 本実施形態のミキサを配置した場合の配管内の流速を示すベクトル線図である。It is a vector diagram which shows the flow velocity in piping at the time of arrange | positioning the mixer of this embodiment. ミキサを使用しない場合のSCR触媒入口におけるアンモニアの濃度分布を示す等濃度線図である。It is an isoconcentration diagram which shows the concentration distribution of ammonia in the SCR catalyst inlet when not using a mixer. 本実施形態のミキサを配置した場合のSCR触媒入口におけるアンモニアの濃度分布を示す等濃度線図である。It is an isoconcentration diagram which shows the density | concentration distribution of ammonia in the SCR catalyst inlet at the time of arrange | positioning the mixer of this embodiment. ミキサの第1の別態様を示す斜視図である。It is a perspective view which shows the 1st another aspect of a mixer. ミキサの第2の別態様を示す側面図である。It is a side view which shows the 2nd another aspect of a mixer. ミキサの第2の別態様を示す斜視図である。It is a perspective view which shows the 2nd another aspect of a mixer.

以下、本発明の実施形態について、図面を用いて詳細に説明する。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

図1に示すように、本実施形態の排気浄化装置1は、車両(図示せず)の動力源となるディーゼルエンジン(内燃機関)101の排気系に設置されている。   As shown in FIG. 1, the exhaust purification device 1 of the present embodiment is installed in an exhaust system of a diesel engine (internal combustion engine) 101 serving as a power source for a vehicle (not shown).

本実施形態の排気浄化装置1は、酸化触媒2、PM(粒子状物質)フィルタ3、インジェクタ(噴射ノズル)4、ミキサ(撹拌手段)5、SCR触媒(選択還元形触媒)6、ASC触媒(アンモニアスリップ防止触媒)7を備えている。   The exhaust purification apparatus 1 of this embodiment includes an oxidation catalyst 2, a PM (particulate matter) filter 3, an injector (injection nozzle) 4, a mixer (stirring means) 5, an SCR catalyst (selective reduction catalyst) 6, an ASC catalyst ( An ammonia slip prevention catalyst) 7 is provided.

ディーゼルエンジン101には、インタークーラ102付きターボチャージャ103が設置され、ターボチャージャ103のタービン出口104に排気浄化装置1が設置されている。つまり、タービン出口104には、連通管部11を通じて、第1チャンバ部12が連通し、この第1チャンバ部12内には、酸化触媒2とPMフィルタ3が配置されている。そして、第1チャンバ部12の出口部には、排気ガスの流れる方向を反転する180度の第1エルボ部13が連通し、この第1エルボ部13の出口部には、直線状の直線状管部(排気管)14が連通している。ここで、第1エルボ部13の出口部内には、インジェクタ4が配置されるとともに、直線状管部14の入口側には、ミキサ5が配置されている。直線状管部14の出口部には、排気ガスの流れる方向を再度反転する180度の第2エルボ部(湾曲管部)15が連通し、この第2エルボ部15の出口部には、第2チャンバ部16が連通している。ここで、第2チャンバ部16内には、SCR触媒6とASC触媒7が、配置されている。そして、第2チャンバ部16の出口部には、排気ガスの流れる方向を再度反転する180度の第3エルボ部17が連通し、この第3エルボ部17の出口部には、外気に通じる連通管部18が連通している。   A turbocharger 103 with an intercooler 102 is installed in the diesel engine 101, and an exhaust purification device 1 is installed at a turbine outlet 104 of the turbocharger 103. That is, the first chamber portion 12 communicates with the turbine outlet 104 through the communication pipe portion 11, and the oxidation catalyst 2 and the PM filter 3 are disposed in the first chamber portion 12. The first elbow part 13 of 180 degrees that reverses the flow direction of the exhaust gas communicates with the outlet part of the first chamber part 12, and the outlet part of the first elbow part 13 has a linear straight line shape. A pipe part (exhaust pipe) 14 is in communication. Here, the injector 4 is disposed in the outlet portion of the first elbow portion 13, and the mixer 5 is disposed on the inlet side of the linear tube portion 14. The outlet portion of the straight tube portion 14 communicates with a 180 ° second elbow portion (curved tube portion) 15 that reverses the flow direction of the exhaust gas again, and the outlet portion of the second elbow portion 15 has a first elbow portion. The two-chamber part 16 communicates. Here, the SCR catalyst 6 and the ASC catalyst 7 are arranged in the second chamber portion 16. A 180 ° third elbow part 17 that reverses the flow direction of the exhaust gas again communicates with the outlet part of the second chamber part 16, and the outlet part of the third elbow part 17 communicates with the outside air. The pipe part 18 communicates.

ディーゼルエンジン101から排出される排気ガスには、一酸化炭素(CO)、炭化水素化合物(HC)、窒素酸化物(NOx)、粒子状物質(PM)が含まれている。そして、排気ガス中のCOとHCが、排気ガスが酸化触媒2を通過する際に化合して、二酸化炭素(CO)と水(HO)が生成される。また、排気ガス中のPMは、PMフィルタ3で捕集される。そして、PMが捕集された排気ガスには、インジェクタ4によって尿素水タンク4aから供給される尿素水(添加物)が噴射される。ここで、噴射された尿素水中の尿素は、排気ガスの熱によって加水分解され、アンモニア(NH)が生成される。そして、このNHとNOxが、SCR触媒6を通過する際に化合して、窒素(N)とHOが生成される。また、排気ガス中に残ったNHは、ASC触媒7を通過する際に、排気ガス中の酸素(O)と化合してNとHOに無毒化されて外気に放出される。 The exhaust gas discharged from the diesel engine 101 contains carbon monoxide (CO), hydrocarbon compounds (HC), nitrogen oxides (NOx), and particulate matter (PM). Then, CO and HC in the exhaust gas are combined when the exhaust gas passes through the oxidation catalyst 2 to generate carbon dioxide (CO 2 ) and water (H 2 O). Further, PM in the exhaust gas is collected by the PM filter 3. And the urea water (additive) supplied from the urea water tank 4a by the injector 4 is injected into the exhaust gas from which PM is collected. Here, urea in the injected urea water is hydrolyzed by the heat of the exhaust gas, and ammonia (NH 3 ) is generated. The NH 3 and NOx combine when passing through the SCR catalyst 6 to generate nitrogen (N 2 ) and H 2 O. Further, when NH 3 remaining in the exhaust gas passes through the ASC catalyst 7, it is combined with oxygen (O 2 ) in the exhaust gas, detoxified into N 2 and H 2 O, and released to the outside air. .

次に、ミキサ5の構成について説明する。本実施形態のミキサ5は、図2〜図5に示すように、排気ガスの流れを整える整流部51と、直線状管部14内にミキサ5を保持する支持部52と、排気ガスの流れを旋回流に変える旋回部53とを備えている。   Next, the configuration of the mixer 5 will be described. As shown in FIGS. 2 to 5, the mixer 5 of the present embodiment includes a rectifying unit 51 that regulates the flow of exhaust gas, a support unit 52 that holds the mixer 5 in the straight tube portion 14, and a flow of exhaust gas. And a swivel portion 53 that turns the swirl into a swirl flow.

整流部51は、平板状部材からなる6枚の整流片51aで構成され、排気ガスの流れ方向となる、直線状管部14の中心軸Oの軸方向に沿って、整流片51aの各板面が配置される。そして、各整流片51aは、直線状管部14の中心軸Oから径方向外側に沿って配置されるとともに、周方向に対して等角度間隔に配置される。また、整流片51aの径方向寸法51Lは、直線状管部14の半径rよりも小さく設定されている。   The rectifying unit 51 is composed of six rectifying pieces 51a made of a flat plate-like member, and each plate of the rectifying pieces 51a along the axial direction of the central axis O of the straight tube part 14 that is the exhaust gas flow direction. A plane is placed. And each rectification | straightening piece 51a is arrange | positioned along the radial direction outer side from the central axis O of the linear pipe part 14, and is arrange | positioned at equal angular intervals with respect to the circumferential direction. Further, the radial dimension 51L of the rectifying piece 51a is set to be smaller than the radius r of the straight tube portion 14.

支持部52は、各整流片51aの径方向外側端から径方向外側に沿って板状に延設されつつ、板面が直線状管部14の内壁面14aに沿って折曲げられることで形成される。そして、支持部52の板面が内壁面14aに当接することで、ミキサ5は直線状管部14内に保持される。   The support portion 52 is formed by bending the plate surface along the inner wall surface 14a of the straight tube portion 14 while extending in a plate shape from the radially outer end of each rectifying piece 51a along the radially outer side. Is done. The mixer 5 is held in the straight tube portion 14 by the plate surface of the support portion 52 coming into contact with the inner wall surface 14a.

旋回部53は、各整流片51aの下流側端に延設され、中心軸Oの軸方向に対して所定の角度に傾けて形成される。また、旋回部53は、扇形状を備え、扇の要部分が直線状管部14の中心軸Oに対応しつつ、扇の円弧縁53bが内壁面14aに面するように形成される。そして、旋回部53は、図3に示すように、断面視で、扇の直線縁53a が隣接する整流片51aに接するように扇形状、および中心軸Oの軸方向に対する傾き角度が設定されている。   The swivel portion 53 extends at the downstream end of each rectifying piece 51 a and is formed to be inclined at a predetermined angle with respect to the axial direction of the central axis O. Moreover, the turning part 53 has a fan shape, and is formed so that the main part of the fan corresponds to the central axis O of the straight tube part 14 and the arc edge 53b of the fan faces the inner wall surface 14a. Then, as shown in FIG. 3, the swivel unit 53 has a fan shape and an inclination angle with respect to the axial direction of the central axis O so that the straight edge 53a of the fan is in contact with the adjacent rectifying piece 51a in a sectional view. Yes.

つまり、本実施形態のミキサ5は、整流片51a、支持部52、旋回部53を備えた板状部材からなる単位構成材5aを6枚備えている。これら単位構成材5aは、直線状管部14の中心軸Oを挟んで対向する整流部51同士が、連結部54によって連結され、連結された2枚の単位構成材5aは、1枚の複合構成材5bを構成する。つまり、本実施形態のミキサ5は、図5に示すように、3枚の複合構成材5bによって構成されている。各複合構成材5bは、連結部54によって、2枚の単位構成材5aが、中心軸Oを対称軸とする線対称に連結されている。なお、各複合構成材5bの連結部54は、整流部51の上流側、中央側、下流側をそれぞれ連結しており、ミキサ5に組上げる際に、これら連結部54が干渉しないように、複合構成材5bが組まれる。   That is, the mixer 5 of the present embodiment includes six unit constituent members 5 a made of a plate-like member including the rectifying piece 51 a, the support portion 52, and the turning portion 53. In these unit constituent members 5a, the rectifying portions 51 facing each other across the central axis O of the straight tube portion 14 are connected by a connecting portion 54, and the two unit constituent members 5a connected are one composite. The constituent material 5b is configured. That is, the mixer 5 of this embodiment is comprised by the 3 composite component 5b, as shown in FIG. In each composite component 5 b, two unit component members 5 a are connected by a connecting portion 54 in line symmetry with the central axis O as the axis of symmetry. In addition, the connection part 54 of each composite component 5b has connected the upstream side of the rectification | straightening part 51, the center side, and the downstream side, respectively, and when assembling to the mixer 5, these connection parts 54 do not interfere. The composite component 5b is assembled.

上記構成によって、ミキサ5を直線状管部14内に設置した際に、整流片51aの径方向外側端部と直線状管部14の内壁面14aとの間、および旋回部53の円弧縁53bと直線状管部14の内壁面14aとの間のそれぞれに、周方向に対して径方向寸法が一定に設定された隙間14b,14cが形成される。   With the above configuration, when the mixer 5 is installed in the straight tube portion 14, the arc edge 53 b between the radially outer end of the rectifying piece 51 a and the inner wall surface 14 a of the straight tube portion 14 and the swivel portion 53. And the inner wall surface 14a of the straight tube portion 14 are formed with gaps 14b and 14c having a constant radial dimension with respect to the circumferential direction.

そして、ミキサ5が直線状管部14内に設置されることによって、排気ガスが直線状管部14内を流れる際に、直線状管部14内には、図2に示すように、直進流路21と旋回流路22が形成される。   Then, by installing the mixer 5 in the straight tube portion 14, when exhaust gas flows through the straight tube portion 14, the straight tube portion 14 has a straight flow as shown in FIG. A path 21 and a swirl flow path 22 are formed.

直進流路21は、ミキサ5と直線状管部14の内壁面14aとの間の隙間によって、直線状管部14内の内壁面14a近傍に筒状に形成される。つまり、直進流路21は、整流部51と内壁面14aとの間に形成される隙間14bと、旋回部53と内壁面14aとの間に形成される隙間14cを流れる排気ガスによって、隙間14b,14cの下流側に形成される。そして、直進流路21には、排気ガスが直線状管部14の中心軸Oの軸方向に沿って流れる。   The straight flow path 21 is formed in a cylindrical shape in the vicinity of the inner wall surface 14 a in the straight tube portion 14 by a gap between the mixer 5 and the inner wall surface 14 a of the straight tube portion 14. That is, the straight flow path 21 has a gap 14b due to the exhaust gas flowing through the gap 14b formed between the rectifying unit 51 and the inner wall surface 14a and the gap 14c formed between the turning unit 53 and the inner wall surface 14a. , 14c on the downstream side. Then, the exhaust gas flows along the axial direction of the central axis O of the straight tube portion 14 in the straight passage 21.

旋回流路22は、直進流路21の筒内側に形成される。つまり、旋回流路22は、直線状管部14の旋回部53下流側に形成される。そして、旋回流路22には、排気ガスが直線状管部14の中心軸Oの軸方向に対して旋回しつつ流れる。   The swirl flow path 22 is formed inside the cylinder of the straight flow path 21. That is, the swirl flow path 22 is formed on the downstream side of the swirl portion 53 of the straight tube portion 14. Then, the exhaust gas flows in the swirl flow path 22 while swirling with respect to the axial direction of the central axis O of the straight tube portion 14.

図6、図7は、直線状管部14と第2エルボ部15を排気ガスが流れる様子を示しており、矢印の向きが流れの方向、矢印の長さが流れの速さを表している。ミキサを設置しない場合には、図6に示すように、直線状管部14の下方では流速が遅く、上方で流速が早くなる。このため、第2エルボ部15では、流速の速い上方の流れが、そのままSCR触媒6に流れ込み、SCR触媒6入口の各部における流速には、大きな差が生じている。   6 and 7 show a state in which the exhaust gas flows through the straight tube portion 14 and the second elbow portion 15, the direction of the arrow indicates the direction of the flow, and the length of the arrow indicates the speed of the flow. . In the case where no mixer is installed, as shown in FIG. 6, the flow velocity is low below the straight tube portion 14, and the flow velocity is high above. For this reason, in the second elbow portion 15, the upper flow having a high flow velocity flows into the SCR catalyst 6 as it is, and there is a large difference in the flow velocity at each portion of the SCR catalyst 6 inlet.

これに対して、ミキサ5を直線状管部14に設置した場合には、図7に示すように、内壁面14a周辺に形成される直進流路21の流速が速く、旋回流路22の流速が遅くなる。このため、第2エルボ部15で排気ガスの流れる方向が反転する際に、第2エルボ部15内で流れが乱れ、SCR触媒6入口における流速分布が改善されている。   On the other hand, when the mixer 5 is installed in the straight pipe portion 14, the flow velocity of the straight passage 21 formed around the inner wall surface 14a is high as shown in FIG. Becomes slower. For this reason, when the flow direction of the exhaust gas in the second elbow part 15 is reversed, the flow is disturbed in the second elbow part 15 and the flow velocity distribution at the inlet of the SCR catalyst 6 is improved.

図8、図9は、SCR触媒6入口におけるアンモニア濃度を示す等濃度線図で、図中に線の数が多いほど濃度差が大きいことを表している。ミキサ5を設置しない場合には、図8に示すように、インジェクタ4から噴射された尿素水が撹拌されないまま直線状管部14内を流れるため、アンモニアの濃い部分と薄い部分が生じている。   FIGS. 8 and 9 are isoconcentration diagrams showing the ammonia concentration at the inlet of the SCR catalyst 6, and the concentration difference increases as the number of lines increases. When the mixer 5 is not installed, as shown in FIG. 8, the urea water injected from the injector 4 flows through the straight pipe portion 14 without being agitated, so that a thick portion and a thin portion of ammonia are generated.

これに対して、ミキサ5を直線状管部14に設置した場合には、図9に示すように、インジェクタ4から噴射された尿素水が、ミキサ5によって撹拌され、SCR触媒6入口におけるアンモニア濃度分布が改善されている。   On the other hand, when the mixer 5 is installed in the straight tube portion 14, as shown in FIG. 9, the urea water injected from the injector 4 is stirred by the mixer 5, and the ammonia concentration at the inlet of the SCR catalyst 6 is obtained. Distribution has been improved.

以上のことから、ミキサ5を直線状管部14に設置したことによって、第2エルボ部15で排気ガスの流れる方向が反転する際に、第2エルボ部15内で流れが乱れ、SCR触媒6入口における流速分布を改善することができる。また、インジェクタ4から噴射される尿素水が、ミキサ5によって発生する流れによって撹拌され、SCR触媒6入口における添加剤濃度分布を改善することができる。   From the above, by installing the mixer 5 in the straight tube portion 14, when the direction of the exhaust gas flow is reversed in the second elbow portion 15, the flow is disturbed in the second elbow portion 15, and the SCR catalyst 6 The flow velocity distribution at the inlet can be improved. Further, the urea water injected from the injector 4 is agitated by the flow generated by the mixer 5, and the additive concentration distribution at the inlet of the SCR catalyst 6 can be improved.

つまり、直線状管部14内で、旋回流は、直進流にぶつかりつつ、旋回を続けるため、アンモニアは内壁面14aに付着せずに排気ガス中に撹拌される。これによって、アンモニアが均一に分布するとともに、直線状管部14の内壁に付着、堆積する尿素が減少し、排気系部品における腐食の発生を抑制することができる。また、隙間14b,14cの径方向寸法を周方向に対して一定に設定することによって、形成される直進流路が安定し、内壁に付着、堆積する尿素をさらに減らすことができる。そして、噴射された尿素水が内壁に付着しないことから、噴射後、時間差なくアンモニアに加水分解されるため、アンモニア濃度を高い精度で制御することができる。これによって、インジェクタ4が必要十分な量の尿素水を噴射することになるため、尿素水の浪費が改善される。   That is, in the straight tube portion 14, the swirling flow continues to swirl while colliding with the straight flow, so that ammonia is not affixed to the inner wall surface 14a but is stirred into the exhaust gas. As a result, ammonia is evenly distributed, and urea that adheres to and accumulates on the inner wall of the straight tube portion 14 is reduced, and the occurrence of corrosion in the exhaust system parts can be suppressed. In addition, by setting the radial dimensions of the gaps 14b and 14c to be constant with respect to the circumferential direction, the formed straight flow path can be stabilized, and urea deposited and deposited on the inner wall can be further reduced. Since the injected urea water does not adhere to the inner wall, it is hydrolyzed to ammonia without time difference after the injection, so that the ammonia concentration can be controlled with high accuracy. Thereby, since the injector 4 injects a necessary and sufficient amount of urea water, waste of urea water is improved.

板状の整流部51を排気ガスの流れ方向に沿って配置することによって、排気ガスの流れを妨げることなく、流れを整えることができ、下流側に形成される旋回流を安定させることができるとともに、整流部51を平板状部材で構成することによって、製造コストを増大させることなく排気ガスを整流することができる。   By arranging the plate-like rectifying unit 51 along the flow direction of the exhaust gas, the flow can be adjusted without disturbing the flow of the exhaust gas, and the swirl flow formed on the downstream side can be stabilized. In addition, the exhaust gas can be rectified without increasing the manufacturing cost by configuring the rectification unit 51 with a flat plate member.

そして、整流部51の下流側に旋回部53を設けることによって、整流された後に旋回するため、整った旋回流が発生し、排気ガスの撹拌を促進させることができる。また、複数の旋回部57が直線状管部14内に等角度間隔で配置されることによって、下流側に形成される旋回流を安定させることができる。   And by providing the swirl | swivel part 53 in the downstream of the rectification | straightening part 51, since it swirls after rectifying | straightening, the prepared swirl | flow flow generate | occur | produces and it can promote stirring of exhaust gas. Further, the plurality of swirling portions 57 are arranged at equal angular intervals in the straight tube portion 14, so that the swirling flow formed on the downstream side can be stabilized.

流れ方向に面して形成された板状の支持部52の板面が、内壁面14aに当接することで、排気ガスの流れを妨げることなく、ミキサ5を直線状管部14内に保持することができる。   The plate surface of the plate-like support portion 52 formed facing the flow direction is in contact with the inner wall surface 14a, so that the mixer 5 is held in the straight tube portion 14 without hindering the flow of exhaust gas. be able to.

複合構成材5bの各連結部54が、整流部51の上流側、中央側、下流側にずれていることで、ミキサ5を組立てる際の誤組付けを防止することができる。   Since each connecting portion 54 of the composite component 5b is shifted to the upstream side, the center side, and the downstream side of the rectifying unit 51, it is possible to prevent erroneous assembly when the mixer 5 is assembled.

なお、本実施形態の整流部51は、平板状に形成されているが、ミキサ5を第1エルボ部13の出口部に配置する等の場合には、第1エルボ部13の曲率に合わせて湾曲させる構成としても良い。   In addition, although the rectification | straightening part 51 of this embodiment is formed in flat form, when arrange | positioning the mixer 5 in the exit part of the 1st elbow part 13, etc., it matches with the curvature of the 1st elbow part 13. It is good also as a structure bent.

次に、ミキサ5の第1の別態様について、図面を用いて説明する。なお、上記実施形態と同様の構成については、同一の符号を付し、詳細な説明を省略する。   Next, the 1st another aspect of the mixer 5 is demonstrated using drawing. In addition, about the structure similar to the said embodiment, the same code | symbol is attached | subjected and detailed description is abbreviate | omitted.

上記実施形態のミキサ5が、6枚の単位構成材5aで構成されているのに対して、本別態様のミキサ5Aは、図10に示すように、4枚の単位構成材5aで構成されている点が上記実施形態と異なる。各単位構成材5aは、上記実施形態と同様に、整流部51、支持部52、旋回部53で構成され、連結部によって2枚一組の複合構成材に形成されている。   Whereas the mixer 5 of the above embodiment is composed of six unit component members 5a, the mixer 5A of this different aspect is composed of four unit component members 5a as shown in FIG. This is different from the above embodiment. Each unit constituent material 5a is composed of a rectifying portion 51, a support portion 52, and a turning portion 53, as in the above embodiment, and is formed into a set of two composite constituent materials by a connecting portion.

また、本態様のミキサ5Aも、上記実施形態と同様に、断面視で、扇の直線縁53a が隣接する整流片51aに接するように設定されている。ところが、本態様のミキサ5Aは、4枚の単位構成材5aで構成されるため、隣接する単位構成材5aとの角度間隔が、上記実施形態よりも広くなる。そこで、断面視で、扇の直線縁53a が隣接する整流片51aに接するように、扇形状、および中心軸Oの軸方向に対する傾き角度が設定されている。   The mixer 5A of this aspect is also set so that the straight edge 53a of the fan contacts the adjacent rectifying piece 51a in a cross-sectional view, as in the above embodiment. However, since the mixer 5A of this aspect is composed of four unit constituent members 5a, the angular interval between the adjacent unit constituent members 5a is wider than that in the above embodiment. Therefore, in the cross-sectional view, the fan shape and the inclination angle of the central axis O with respect to the axial direction are set so that the straight edge 53a of the fan is in contact with the adjacent rectifying piece 51a.

以上のことから、本態様のミキサ5Aは、上記実施形態と同様の作用効果が得られる。また、単位構成材5aの枚数が少ないことから、排気ガスの流量が小さく、排気管の管径が小さくなる、排気量が比較的小さいディーゼルエンジン101の排気浄化装置として好適である。   From the above, the mixer 5A of this aspect can obtain the same effects as the above embodiment. Further, since the number of unit constituent members 5a is small, it is suitable as an exhaust emission control device for the diesel engine 101 with a small exhaust gas flow rate, a small exhaust pipe diameter, and a relatively small exhaust amount.

次に、ミキサ5の第2の別態様について、図面を用いて説明する。なお、上記実施形態と同様の構成については、同一の符号を付し、詳細な説明を省略する。   Next, a second alternative embodiment of the mixer 5 will be described with reference to the drawings. In addition, about the structure similar to the said embodiment, the same code | symbol is attached | subjected and detailed description is abbreviate | omitted.

本態様のミキサ5Bは、5枚の複合構成材で構成されている。上記実施形態のミキサ5では、複合構成材5bが、2枚の単位構成材5aを連結部54で連結することで構成されているのに対して、本別態様のミキサ5Bでは、図11、図12に示すように、整流片55a(整流部55)と旋回部56で構成される単位構成材が整流片55b(整流部55)に連結されることで、複合構成材が構成されている。つまり、組立てられた状態のミキサ5Bは、旋回部56が延設された整流片55aと旋回部56を有しない整流片55bが、周方向に対して交互に配置される。なお、整流片55aの軸方向寸法55Laは、整流片55bの軸方向寸法55Lbよりも長くなるように設定されている。   The mixer 5B of this aspect is composed of five composite components. In the mixer 5 of the above embodiment, the composite constituent material 5b is configured by connecting the two unit constituent materials 5a with the connecting portion 54, whereas in the mixer 5B of this different aspect, FIG. As shown in FIG. 12, a unit constituent material composed of a rectifying piece 55a (rectifying portion 55) and a turning portion 56 is connected to a rectifying piece 55b (rectifying portion 55), thereby forming a composite constituent material. . That is, in the assembled mixer 5B, the rectifying pieces 55a with the swivel portions 56 extended and the rectifying pieces 55b without the swivel portions 56 are alternately arranged in the circumferential direction. The axial dimension 55La of the rectifying piece 55a is set to be longer than the axial dimension 55Lb of the rectifying piece 55b.

また、旋回部56の円弧縁には、切欠57によって段差が形成されている。この切欠57を設けることで、直線状管部14の内壁面14aとミキサ5Bとの間に隙間が形成され、この隙間を排気ガスが流れることによって、直進流路が形成される。   Further, a step is formed by a notch 57 at the arc edge of the turning portion 56. By providing this notch 57, a gap is formed between the inner wall surface 14a of the straight tube portion 14 and the mixer 5B, and exhaust gas flows through this gap to form a straight passage.

なお、切欠57を整流片55aとの境界部分に設けることで、上記実施形態と同様に、内壁面14aとミキサとの間に環状の隙間と、隙間の下流側に筒状の直進流路を形成することができる。   In addition, by providing the notch 57 at the boundary portion with the rectifying piece 55a, an annular gap is formed between the inner wall surface 14a and the mixer, and a cylindrical straight passage is provided downstream of the gap, as in the above embodiment. Can be formed.

以上のことから、本態様のミキサ5Aは、上記実施形態と同様の作用効果が得られる。   From the above, the mixer 5A of this aspect can obtain the same effects as the above embodiment.

本発明は、ディーゼルエンジンの排気系に利用することができる。   The present invention can be used for an exhaust system of a diesel engine.

1…排気浄化装置
5…撹拌手段(ミキサ)
14…排気管(直線状管部)
14a…内壁面
14c…隙間
21…直進流路
22…旋回流路
51…整流部
52…支持部
53…旋回部
O…中心軸
DESCRIPTION OF SYMBOLS 1 ... Exhaust gas purification device 5 ... Stirring means (mixer)
14 ... Exhaust pipe (straight pipe section)
14a ... Inner wall surface 14c ... Gap 21 ... Straight passage 22 ... Swirl passage 51 ... Rectifying part 52 ... Support part 53 ... Swivel part O ... Center axis

Claims (5)

内燃機関の排気管(14)内に配置される撹拌手段(5)を備えた排気浄化装置(1)であって、
前記撹拌手段(5)は、排気ガスの流れ方向に沿って配置され、排気ガスの流れを整える板状の整流部(51)と、該整流部(51)の下流側に排気ガスを旋回流に変える旋回部(53)とを有し、
前記整流部(51)は複数の整流片(51a)で構成され、
該整流片(51a)の前記排気管(14)の内壁面(14a)に対向する径方向外側端部と前記内壁面(14a)との間に第1の隙間(14b)が形成され、
前記旋回部(53)は、前記整流片(51a)の下流側に扇形状に延設された扇形状部を有し、
該扇形状部の円弧縁(53b)は前記内壁面(14a)に面し、
前記円弧縁(53b)と前記内壁面(14a)とに間に第2の隙間(14c)が形成されると共に
前記第1の隙間(14b)及び前記第2の隙間(14c)は、その径方向寸法が周方向に対して一定に設定され、
前記排気管(14)内を排気ガスが流れる際に、
前記第1の隙間(14b)及び前記第2の隙間(14c)の下流側に筒状に、排気ガスが該排気管(14)の中心軸(O)の軸方向に沿って流れる直進流路(21)と、
該直進流路(21)の筒内側に、排気ガスが該中心軸(O)の該軸方向に対して旋回しつつ流れる旋回流路(22)とが形成されることを特徴とする排気浄化装置。
An exhaust purification device (1) comprising a stirring means (5) disposed in an exhaust pipe (14) of an internal combustion engine,
The stirring means (5) is arranged along the flow direction of the exhaust gas, and has a plate-like rectification part (51) for adjusting the flow of the exhaust gas, and a swirl flow of the exhaust gas downstream of the rectification part (51). A swivel part (53) to be converted into
The rectifying unit (51) is composed of a plurality of rectifying pieces (51a),
A first gap (14b) is formed between the radially outer end of the rectifying piece (51a) facing the inner wall surface (14a) of the exhaust pipe (14) and the inner wall surface (14a),
The swivel part (53) has a fan-shaped part extending in a fan shape on the downstream side of the rectifying piece (51a),
An arc edge (53b) of the fan-shaped portion faces the inner wall surface (14a),
A second gap (14c) is formed between the arc edge (53b) and the inner wall surface (14a) ,
The first gap (14b) and the second gap (14c) are set such that their radial dimensions are constant with respect to the circumferential direction,
When exhaust gas flows through the exhaust pipe (14),
A straight flow path in which the exhaust gas flows in a cylindrical shape downstream of the first gap (14b) and the second gap (14c) along the axial direction of the central axis (O) of the exhaust pipe (14). (21) and
The exhaust gas purification is characterized in that a swirl flow path (22) in which exhaust gas swirls with respect to the axial direction of the central axis (O) is formed inside the cylinder of the straight flow path (21). apparatus.
請求項1に記載の排気浄化装置であって、The exhaust emission control device according to claim 1,
前記撹拌手段(5)を前記排気管(14)の軸方向から視認した場合、前記扇形形状部の直線縁(53a)が、隣接する前記整流片(51a)に接する位置関係に配置されていることを特徴とする排気浄化装置。When the stirring means (5) is viewed from the axial direction of the exhaust pipe (14), the straight edge (53a) of the fan-shaped portion is arranged in a positional relationship in contact with the adjacent rectifying piece (51a). An exhaust purification device characterized by that.
請求項1、または請求項2に記載の排気浄化装置であって、
前記撹拌手段(5)は、前記整流片(51a)から径方向外側に延設される支持部(52)を備え、
該支持部(52)によって、該旋回部(53)は該排気管(14)の前記内壁面(14a)から離間して位置しつつ、該撹拌手段(5)が前記排気管(14)内に保持されることを特徴とする排気浄化装置。
An exhaust emission control device according to claim 1 or claim 2,
The stirring means (5) includes a support portion (52) extending radially outward from the rectifying piece (51a) ,
The agitating means (5) is located in the exhaust pipe (14) while the swivel part (53) is positioned away from the inner wall surface (14a) of the exhaust pipe (14) by the support part (52). An exhaust emission control device that is held by
請求項1から請求項3のいずれか1項に記載の排気浄化装置であって、
前記撹拌手段(5)は、前記旋回部(53)を複数備え、
該旋回部(53)が、前記中心軸(O)を中心に、周方向に対して等角度間隔で配置されることを特徴とする排気浄化装置。
The exhaust emission control device according to any one of claims 1 to 3,
The stirring means (5) includes a plurality of the swivel portions (53),
The exhaust gas purifying device characterized in that the swivel portions (53) are arranged at equiangular intervals with respect to the circumferential direction around the central axis (O).
請求項1から請求項4のいずれか1項に記載の排気浄化装置であって、An exhaust emission control device according to any one of claims 1 to 4,
前記直進流路(21)の流速は、前記旋回流路(22)の流速より早く、The flow rate of the straight channel (21) is faster than the flow rate of the swirl channel (22),
前記撹拌手段(5)が配設された前記排気管(14)の下流側に触媒が配設されたチャンバ(16)を有し、A chamber (16) in which a catalyst is disposed downstream of the exhaust pipe (14) in which the stirring means (5) is disposed;
前記排気管(14)の出口部と前記チャンバ(16)の入口部との間には、湾曲管(15)を介して接続されているA bent pipe (15) is connected between the outlet of the exhaust pipe (14) and the inlet of the chamber (16).
ることを特徴とする排気浄化装置。An exhaust emission control device characterized by the above.
JP2013158677A 2013-07-31 2013-07-31 Exhaust purification device Active JP6046568B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2013158677A JP6046568B2 (en) 2013-07-31 2013-07-31 Exhaust purification device
CN201420354201.7U CN203978582U (en) 2013-07-31 2014-06-27 Exhaust gas purifying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2013158677A JP6046568B2 (en) 2013-07-31 2013-07-31 Exhaust purification device

Publications (2)

Publication Number Publication Date
JP2015031158A JP2015031158A (en) 2015-02-16
JP6046568B2 true JP6046568B2 (en) 2016-12-14

Family

ID=52516707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2013158677A Active JP6046568B2 (en) 2013-07-31 2013-07-31 Exhaust purification device

Country Status (1)

Country Link
JP (1) JP6046568B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022098386A (en) * 2020-12-21 2022-07-01 株式会社三五 Exhaust emission control system

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4255124A (en) * 1978-10-05 1981-03-10 Baranowski Jr Frank Static fluid-swirl mixing
DE102007035226A1 (en) * 2007-07-25 2009-01-29 J. Eberspächer GmbH & Co. KG Flow guiding device and thus equipped exhaust system
US8397495B2 (en) * 2008-06-26 2013-03-19 Tenneco Automotive Operating Company Inc. Exhaust gas additive/treatment system and mixer for use therein
US9909421B2 (en) * 2009-12-18 2018-03-06 Volvo Truck Corporation Mixing system for an exhaust gases after-treatment arrangement
US20120204541A1 (en) * 2011-02-14 2012-08-16 GM Global Technology Operations LLC Exhaust mixer element and method for mixing
EP2716884A4 (en) * 2011-06-02 2014-12-03 Toyota Motor Co Ltd EXHAUST GAS PURIFYING DEVICE FOR INTERNAL COMBUSTION ENGINE
JP6125248B2 (en) * 2013-01-31 2017-05-10 日野自動車株式会社 Urea water mixing structure

Also Published As

Publication number Publication date
JP2015031158A (en) 2015-02-16

Similar Documents

Publication Publication Date Title
US9909421B2 (en) Mixing system for an exhaust gases after-treatment arrangement
JP5714844B2 (en) Exhaust gas purification device
US11583812B2 (en) Mixer assembly for vehicle exhaust system
US10086333B2 (en) Dual auger mixing system
US10443477B2 (en) Counter-swirl mixer
CN102159810B (en) Mixing device in the exhaust pipe
US11428140B1 (en) Mixer assembly for vehicle exhaust system
US10486117B2 (en) Method, apparatus and system for aftertreatment of exhaust gas comprising inline housing
WO2011110885A1 (en) Mixing system for an exhaust gas after-treatment arrangement
US10252225B2 (en) Method, apparatus and mixing device for evenly mixing reactant to exhaust gas flow
US20090266064A1 (en) Exhaust gas additive/treatment system and mixer for use therein
US20150308316A1 (en) Integrated mixing system for exhaust aftertreatment system
JP6046568B2 (en) Exhaust purification device
EP3489480B1 (en) Scr mixer and scr device comprising same
KR102195085B1 (en) Mixer for exhaust system
JP6347474B2 (en) Exhaust purification device
JP6077963B2 (en) Exhaust purification device
JP7432240B2 (en) Exhaust purification device, flow path forming member, and cylindrical member
JP7478228B2 (en) Mixing device and method for exhaust aftertreatment
WO2020145101A1 (en) Mixing member, exhaust purifying device, and vehicle

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20150911

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20160427

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20160510

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20160708

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20161115

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20161117

R150 Certificate of patent or registration of utility model

Ref document number: 6046568

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S343 Written request for registration of root pledge or change of root pledge

Free format text: JAPANESE INTERMEDIATE CODE: R316354

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

SZ02 Written request for trust registration

Free format text: JAPANESE INTERMEDIATE CODE: R316Z02

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S803 Written request for registration of cancellation of provisional registration

Free format text: JAPANESE INTERMEDIATE CODE: R316803

SZ02 Written request for trust registration

Free format text: JAPANESE INTERMEDIATE CODE: R316Z02

SZ03 Written request for cancellation of trust registration

Free format text: JAPANESE INTERMEDIATE CODE: R316Z03

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250