JPH0718332B2 - Device for separating dust from engine exhaust gas - Google Patents

Device for separating dust from engine exhaust gas

Info

Publication number
JPH0718332B2
JPH0718332B2 JP16497290A JP16497290A JPH0718332B2 JP H0718332 B2 JPH0718332 B2 JP H0718332B2 JP 16497290 A JP16497290 A JP 16497290A JP 16497290 A JP16497290 A JP 16497290A JP H0718332 B2 JPH0718332 B2 JP H0718332B2
Authority
JP
Japan
Prior art keywords
dust
exhaust gas
soot
swirl
end side
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP16497290A
Other languages
Japanese (ja)
Other versions
JPH0454208A (en
Inventor
山口  篤
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP16497290A priority Critical patent/JPH0718332B2/en
Publication of JPH0454208A publication Critical patent/JPH0454208A/en
Publication of JPH0718332B2 publication Critical patent/JPH0718332B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • 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、エンジンの排気ガス中の煤塵分離装置に関す
る。
TECHNICAL FIELD The present invention relates to a device for separating dust from exhaust gas of an engine.

以下、請求項1に記載の発明を「第1発明」、請求項2
に記載の発明を「第2発明」という。
Hereinafter, the invention described in claim 1 is referred to as “first invention” and claim 2
The invention described in (2) is referred to as "second invention".

[基本構造] 第1発明の前提となるエンジンの排気ガス中の煤塵分離
装置の基本構造は、次のようになっている。
[Basic Structure] The basic structure of the device for separating dust from the exhaust gas of an engine, which is the premise of the first invention, is as follows.

例えば第1図または第4図に示すように、 「筒形本体1内の始端側S中央部に排気ガス入口管2
を、終端側E中央部に排気ガス出口管3を連通させ、 筒形本体1内の始端側Sの中央部から周囲部に向かって
順に排気ガス4の旋回案内板5と環状の旋回開始室6と
を設け、 筒形本体1内の終端側Eの周囲部に集塵室7を設け、集
塵室7の始端面8に煤塵入口9をあけて構成した」もの
である。
For example, as shown in FIG. 1 or FIG. 4, “the exhaust gas inlet pipe 2 is provided at the center of the starting end side S in the tubular body 1.
The exhaust gas outlet pipe 3 is communicated with the central portion of the end side E, and the swirl guide plate 5 and the annular swirl start chamber for the exhaust gas 4 are sequentially arranged from the central portion of the start end side S in the tubular main body 1 toward the peripheral portion. 6 is provided, the dust collecting chamber 7 is provided around the terminal end side E in the cylindrical main body 1, and the soot dust inlet 9 is opened at the starting end face 8 of the dust collecting chamber 7. "

すなわち、この種の煤塵分離装置は、第1図(B)また
は第4図(B)に示すように、排気ガス入口管2から流
入する排気ガス4を、旋回案内板5で案内して旋回開始
室6で旋回流23を形成し、そのまま筒形本体1内の旋回
通路30で旋回を繰り返させながら終端側Eに向かって進
行させ、旋回による遠心力の作用で、排気ガス4の成分
のうち、高比重の煤塵21を旋回通路30の周囲側に、低比
重のガス分22を中心側にそれぞれ分離させ、煤塵21を集
塵室7に、ガス分22を排気ガス出口管3にそれぞれ流入
させるようにしたものである。
That is, as shown in FIG. 1 (B) or FIG. 4 (B), this type of dust separation apparatus swirls the exhaust gas 4 flowing from the exhaust gas inlet pipe 2 by means of the swirl guide plate 5. A swirl flow 23 is formed in the start chamber 6, and the swirl passage 30 in the cylindrical main body 1 is repeatedly swirled to move toward the end side E, and the centrifugal force generated by swirling causes the components of the exhaust gas 4 to flow. Among them, the high specific gravity soot dust 21 is separated into the swirl passage 30 peripheral side, and the low specific gravity gas component 22 is separated into the center side, soot dust 21 is provided in the dust collection chamber 7, and gas component 22 is provided in the exhaust gas outlet pipe 3, respectively. It was made to flow in.

[従来の技術] 上記基本構造において、旋回案内板5の形状は、従来で
は第4図(B)に示すように、筒形本体1の軸心12と平
行になるように形成していた。
[Prior Art] In the above basic structure, the shape of the swivel guide plate 5 is conventionally formed so as to be parallel to the axis 12 of the cylindrical main body 1, as shown in FIG. 4 (B).

[発明が解決しようとする課題] 上記従来技術では、煤塵の分離性能が低いという問題が
ある。
[Problems to be Solved by the Invention] In the above-mentioned conventional technology, there is a problem that the separation performance of soot and dust is low.

すなわち、第4図(B)に示すように、筒形本体1の軸
心12と平行になるように形成した旋回案内板5では、排
気ガス入口管2からの排気ガス4を筒形本体1の周方向
に案内する機能しかないため、排気ガス4の旋回流23は
そのピッチが小さくなり、集塵室7に至るまでの旋回回
数が不要に多くなる。
That is, as shown in FIG. 4 (B), in the swirl guide plate 5 formed so as to be parallel to the axis 12 of the tubular body 1, the exhaust gas 4 from the exhaust gas inlet pipe 2 is fed into the tubular body 1. Since there is only a function of guiding the exhaust gas 4 in the circumferential direction, the pitch of the swirling flow 23 of the exhaust gas 4 becomes small, and the number of swirling times to reach the dust collecting chamber 7 unnecessarily increases.

このため、旋回流23の旋回速度が旋回通路30の途中で低
下し、集塵室7付近では遠心力の低下により、一旦分離
された煤塵21がガス分22に再混入されるので、煤塵21の
分離性能が低いのである。
For this reason, the swirling velocity of the swirling flow 23 decreases in the middle of the swirling passage 30, and the soot dust 21 once separated is remixed in the gas component 22 due to the reduction of the centrifugal force in the vicinity of the dust collecting chamber 7. The separation performance of is low.

本発明は、煤塵の分離性能を高めること、をその課題と
する。
An object of the present invention is to improve the separation performance of soot and dust.

[課題を解決するための手段] (第1発明) 第1発明は、上記課題を解決するため、前記基本構造に
おいて、旋回案内板5の形状を次のように形成したこと
を特徴とする。
[Means for Solving the Problem] (First Invention) In order to solve the above problems, the first invention is characterized in that in the basic structure, the turning guide plate 5 is formed as follows.

例えば第1図(B)に示すように、「旋回案内板5の形
状を、その始端部10から終端部11に近づくにつれて筒形
本体1の軸心12からの距離が次第に大きくなる傾斜状に
形成した」ものである。
For example, as shown in FIG. 1 (B), "the shape of the swivel guide plate 5 is formed into an inclined shape in which the distance from the axial center 12 of the tubular main body 1 gradually increases as the starting end 10 approaches the terminal end 11. It was formed.

(第2発明) 第2発明は、例えば第1図(B)に示すように、上記第
1発明において、「旋回案内板5の終端板13から旋回流
案内筒14を終端側Eに向けて突出させ、集塵室7の始端
内周部15から煤塵分離筒16を始端側Sに向けて突出さ
せ、旋回流案内筒14の終端縁17を煤塵分離筒16の始端縁
18の近傍位置19乃至これよりも終端側E寄りの位置20に
位置させた」ものである。
(Second invention) As shown in FIG. 1 (B), for example, in the second invention, in the above first invention, "the swirl flow guide cylinder 14 is directed from the end plate 13 of the swirl guide plate 5 toward the end side E. The dust separation chamber 16 is protruded from the inner peripheral portion 15 of the start end of the dust collection chamber 7 toward the start end side S, and the end edge 17 of the swirl flow guide cylinder 14 is started at the start end edge of the dust separation cylinder 16.
It is located at a position 19 near 18 or a position 20 closer to the terminal end E than this.

[作用] (第1発明) 第1発明は、次のように作用する。[Operation] (First Invention) The first invention operates as follows.

例えば第1図(B)に示すように、傾斜状の旋回案内板
5は、排気ガス入口管2から流入する排気ガス4を筒形
本体1の周方向に案内するとともに、筒形本体1の終端
側Eに偏向させる機能をも有するため、排気ガス4の旋
回流23はそのピッチが大きく、集塵室7に至るまでの旋
回回数が少ない。
For example, as shown in FIG. 1 (B), the inclined swirl guide plate 5 guides the exhaust gas 4 flowing from the exhaust gas inlet pipe 2 in the circumferential direction of the tubular body 1, and The swirling flow 23 of the exhaust gas 4 has a large pitch and has a small number of swirling times to reach the dust collecting chamber 7 because it also has a function of deflecting to the terminal end side E.

このため、旋回流23の旋回速度は集塵室7に至るまで高
速に維持され、遠心力が大きなまま維持されるので、一
旦分離された煤塵21のガス分22への再混入が防止され、
煤塵21の分離性能が高まる。
Therefore, the swirling speed of the swirling flow 23 is maintained at a high speed until reaching the dust collecting chamber 7, and the centrifugal force is kept large, so that the once separated soot dust 21 is prevented from being re-mixed into the gas component 22,
The separation performance of the dust 21 is improved.

(第2発明) 第2発明は、上記第1発明の作用に加え、次のように作
用する。
(2nd invention) In addition to the effect | action of the said 1st invention, a 2nd invention acts as follows.

例えば第1図(B)に示すように、旋回開始室6を出て
から集塵室7に至るまでの旋回通路30の通路断面積は、
旋回流案内筒14により狭められているので、旋回流23の
速度は高速となり、これにより大きな遠心力を生じさせ
ることができ、煤塵21の分離性能が一層高まる。
For example, as shown in FIG. 1 (B), the passage cross-sectional area of the swirl passage 30 from the swirl start chamber 6 to the dust collection chamber 7 is:
Since it is narrowed by the swirling flow guide cylinder 14, the swirling flow 23 has a high speed, which can generate a large centrifugal force and further enhance the separation performance of the soot dust 21.

旋回通路30の周囲側に集まる煤塵21と中央側に集まるガ
ス分22とは煤塵分離筒16で隔離されるので、一旦分離し
た煤塵21がガス分22により排気ガス出口管3に連れ込ま
れるのを防止でき、煤塵の分離性能が一層高まる。
The soot dust 21 that collects on the peripheral side of the swirl passage 30 and the gas component 22 that collects on the center side are separated by the soot dust separating cylinder 16, so that the soot dust 21 that has once been separated is taken into the exhaust gas outlet pipe 3 by the gas component 22. It can be prevented and the separation performance of soot and dust is further enhanced.

[効果] (第1発明) 第1発明は、次の効果・を奏する。[Effects] (First Invention) The first invention has the following effects.

煤塵の分離性能が高まる。The separation performance of soot and dust is improved.

排気ガスの旋回流はそのピッチが大きく、集塵室に至る
までの旋回回数が不要に多くなることがなく、これによ
り旋回流の旋回速度は集塵室に至るまで高速に維持さ
れ、遠心力が大きなまま維持されるので、一旦分離され
た煤塵のガス分へ再混入が防止され、煤塵の分離性能が
高まるのである。
The swirling flow of exhaust gas has a large pitch, and the number of times of swirling to reach the dust collecting chamber does not unnecessarily increase, which allows the swirling speed of the swirling flow to be maintained at a high speed until reaching the dust collecting chamber, and the centrifugal force Is maintained as it is, the re-mixing of the once separated soot dust into the gas component is prevented, and the soot dust separation performance is improved.

簡易かつ安価に実施できる。It can be implemented easily and inexpensively.

旋回案内板の形状を変形するのみでよいため、簡易かつ
安価に実施できるのである。
Since it is only necessary to change the shape of the swivel guide plate, it can be implemented easily and inexpensively.

(第2発明) 第2発明は、上記第1発明の効果・に加え、次の効
果をも奏する。
(Second Invention) The second invention has the following effects in addition to the effects of the first invention.

煤塵分離性能が一層高まる。The dust separation performance is further enhanced.

旋回通路の通路断面積は、旋回流案内筒により狭められ
ているので、旋回流の速度は高速となり、これにより大
きな遠心力を生じさせることができる。
Since the passage cross-sectional area of the swirl passage is narrowed by the swirl flow guide tube, the swirl flow velocity becomes high, and thereby a large centrifugal force can be generated.

旋回通路の周囲側に集まる煤塵と中央側に集まるガス分
とは煤塵分離筒で隔離されるので、一旦分離した煤塵が
ガス分により排気ガス出口管に連れ込まれるのを防止で
きる。
Since the soot dust collected on the peripheral side of the swirl passage and the gas component collected on the center side are separated by the soot dust separating cylinder, it is possible to prevent the once separated soot dust from being taken into the exhaust gas outlet pipe by the gas component.

このため、煤塵の分離性能が一層高まるのである。Therefore, the separation performance of soot and dust is further enhanced.

[実施例] 本発明の実施例を図面に基づいて説明する。[Embodiment] An embodiment of the present invention will be described with reference to the drawings.

第1図において、符号24は煤塵分離装置を示しており、
この煤塵分離装置24はエンジンの排気経路中に介在さ
せ、排気ガス4を煤塵21とガス分22とに分離し、煤塵21
を集塵室7に集めるためのものである。
In FIG. 1, reference numeral 24 indicates a dust separator,
The soot / dust separator 24 is interposed in the exhaust path of the engine to separate the exhaust gas 4 into soot / dust 21 and gas component 22.
To collect in the dust collection chamber 7.

第1図(A)・(B)に示すように、この煤塵分離装置
24は、筒形本体1内の始端側S中央部に排気ガス入口管
2を、終端側E中央部に排気ガス出口管3を連通させて
構成してある。
As shown in FIGS. 1 (A) and (B), this dust separation device
In the tubular body 1, the exhaust gas inlet pipe 2 is connected to the center of the starting end side S and the exhaust gas outlet pipe 3 is connected to the center of the end end E.

筒形本体1内の始端側Sには、その中央部から周囲部に
向かって順に排気ガス4の旋回案内板5と環状の旋回開
始室6とを設けており、旋回案内板5と旋回開始室6と
は具体的には次のように構成してある。
A swirl guide plate 5 and an annular swirl start chamber 6 for the exhaust gas 4 are provided on the starting end side S in the cylindrical main body 1 in this order from the central portion toward the peripheral portion. The chamber 6 is specifically configured as follows.

すなわち、筒形本体1内の始端側Sの中央部に排気ガス
入口管2を挿入し、排気ガス入口管2の周壁に軸方向長
手状の複数の排気ガス流出口25を形成し、第1図(C)
に示すように、排気ガス流出口25から流出される排気ガ
ス4を筒形本体1の周方向に案内する湾曲状の旋回案内
板5を排気流出口25に臨ませて排気ガス入口管2の外周
壁に付設し、この旋回案内板5に案内された排気ガス4
が流れ込む旋回案内板5の周囲空間をそのまま旋回開始
室6として利用している。
That is, the exhaust gas inlet pipe 2 is inserted into the central portion of the starting end side S in the cylindrical main body 1, and a plurality of exhaust gas outlets 25 which are longitudinal in the axial direction are formed on the peripheral wall of the exhaust gas inlet pipe 2. Figure (C)
As shown in, the curved swirl guide plate 5 for guiding the exhaust gas 4 flowing out from the exhaust gas outlet 25 in the circumferential direction of the cylindrical main body 1 is faced to the exhaust outlet 25 and the exhaust gas inlet pipe 2 Exhaust gas 4 attached to the outer peripheral wall and guided by the swivel guide plate 5
The space around the swirl guide plate 5 into which the air flows is used as the swirl start chamber 6 as it is.

第1図(A)・(B)に示すように、筒形本体1内の終
端側Eの周囲部には、集塵室7を設け、集塵室7の始端
面8に煤塵入口9をあけて構成しており、集塵室7と煤
塵入口9とは具体的には次のように構成してある。
As shown in FIGS. 1 (A) and 1 (B), a dust collecting chamber 7 is provided around the terminal end side E in the cylindrical main body 1, and a dust inlet 9 is provided on a starting end face 8 of the dust collecting chamber 7. The dust collection chamber 7 and the soot dust inlet 9 are specifically configured as follows.

すなわち、筒形本体1内の終端側Eの中央部に排気ガス
出口管3を挿入し、その外周に形成した筒状の集塵室内
周壁26と円環状の集塵室始端壁27とで筒形本体1内の終
端側Eの隅部に円環状の集塵室7を形成し、集塵室始端
壁27の上側部に煤塵入口9をあけてある。
That is, the exhaust gas outlet pipe 3 is inserted into the central portion of the end side E in the cylindrical main body 1, and a cylindrical dust collecting chamber peripheral wall 26 and an annular dust collecting chamber starting end wall 27 formed on the outer periphery of the exhaust gas outlet pipe 3 form a cylinder. An annular dust collecting chamber 7 is formed in a corner portion on the terminal end side E in the main body 1, and a dust inlet 9 is opened in an upper portion of the dust collecting chamber starting end wall 27.

集塵室7の外周側面下部に煤塵取出口28をあけ、煤塵取
出口28はプラグ29で開閉可能としてあるが、この煤塵取
出口28は煤塵処理器(図外)に連通させておいてもよ
い。
A soot dust outlet 28 is opened in the lower part of the outer peripheral side surface of the dust collecting chamber 7, and the soot dust outlet 28 can be opened and closed by a plug 29. However, even if this soot dust outlet 28 is communicated with a soot dust processing device (not shown) Good.

上述の構成から明らかなように、この煤塵分離装置24
は、第1図(B)に示すように、排気ガス入口管2から
流入する排気ガス4を、旋回案内板5で案内して旋回開
始室6で旋回流23を形成し、そのまま筒形本体1内の旋
回通路30で旋回を繰り返させながら終端側Eに向かって
進行させ、旋回による遠心力の作用で、排気ガス4の成
分のうち、高比重の煤塵21を旋回通路30の周囲側に、低
比重のガス分22を中心側にそれぞれ分離させ、煤塵21を
集塵室7に、ガス分22を排気ガス出口管3にそれぞれ流
入させるようにしたものである。
As is clear from the above configuration, this dust separation device 24
As shown in FIG. 1 (B), the swirl guide plate 5 guides the exhaust gas 4 flowing in from the exhaust gas inlet pipe 2 to form the swirl flow 23 in the swirl start chamber 6, and the tubular body is maintained as it is. In the swirl passage 30 in 1 while advancing toward the terminal end E while repeating swirl, the centrifugal force caused by swirling causes the dust 21 having a high specific gravity among the components of the exhaust gas 4 to flow around the swirl passage 30. The low-specific-gravity gas component 22 is separated toward the center side, and the soot dust 21 is caused to flow into the dust collection chamber 7, and the gas component 22 is caused to flow into the exhaust gas outlet pipe 3, respectively.

煤塵21とガス分22との分離性能を高めるため、旋回案内
板5の形状はその始端部10から終端部11に近づくにつれ
て筒形本体1の軸心12からの距離が次第に大きくなる傾
斜状に形成し、排気ガス入口管2から流入する排気ガス
4を筒形本体1の終端側Eに偏向させ、排気ガス4の旋
回流23のピッチを大きくし、集塵室7に至るまでの旋回
回数が不要に多くならないようにし、これにより旋回流
23の旋回速度を集塵室7に至るまで高速に維持し、遠心
力を大きなまま維持するようにしてある。
In order to improve the separation performance between the soot dust 21 and the gas component 22, the shape of the swivel guide plate 5 is an inclined shape in which the distance from the axial center 12 of the cylindrical main body 1 gradually increases as the starting end 10 approaches the terminal end 11. The number of times of swirling until the dust collecting chamber 7 is formed by increasing the pitch of the swirling flow 23 of the exhaust gas 4 by forming the exhaust gas 4 flowing from the exhaust gas inlet pipe 2 and deflecting the exhaust gas 4 toward the terminal end side E of the cylindrical main body 1. Of the swirling flow
The turning speed of 23 is maintained at a high speed up to the dust collecting chamber 7, and the centrifugal force is kept large.

より大きな遠心力を生じさせるため、旋回案内板5の終
端板13から旋回流案内筒14を終端側Eに向けて突出させ
ることにより、旋回通路30の通路断面積を旋回流案内筒
14により狭め、旋回流23の速度が高速となるようにして
ある。
In order to generate a larger centrifugal force, the swirl flow guide cylinder 14 is projected from the end plate 13 of the swirl guide plate 5 toward the terminal end side E, so that the passage cross-sectional area of the swirl passage 30 is changed.
It is made narrower by 14 so that the speed of the swirling flow 23 becomes high.

一旦分離した煤塵21がガス分22により排気ガス出口管3
に連れ込まれるのを防止するため、集塵室7の始端内周
部15から煤塵分離筒16を始端側Sに向けて突出させ、旋
回流案内筒14の終端縁17を煤塵分離筒16の始端縁18の近
傍位置19よりも終端側E寄りの位置20に位置させること
により、周囲側に集まる煤塵21と中心側に集まるガス分
22とを煤塵分離筒16で隔離できるようにしてある。
The soot dust 21 once separated is separated by the gas component 22 into the exhaust gas outlet pipe 3
In order to prevent the dust collection chamber 7 from being brought into the start end, the dust separation cylinder 16 is projected from the inner peripheral portion 15 of the start end toward the start end side S, and the end edge 17 of the swirl flow guide cylinder 14 is started at the start end of the dust separation cylinder 16. By positioning it at a position 20 closer to the terminal end E than the position 19 near the edge 18, the soot dust 21 collecting on the peripheral side and the gas content collecting on the center side
22 and 22 can be isolated by the dust separation cylinder 16.

集塵室7への煤塵21の流入をより確実にするため、第2
図に示すように、集塵室始端壁27の右側が終端側E寄り
に位置するように傾けることにより、集塵室始端壁27の
排気ガス旋回方向の始端縁33の終端縁34よりも筒形本体
1の始端側Sに偏位させ、集塵室始端壁27の始端縁33と
終端縁34との間の離間空間で形成される煤塵入口9の煤
塵21の侵入方向に対する開口幅S1を広げ、その開口断面
積を広げてある。
In order to ensure the inflow of soot dust 21 into the dust collection chamber 7, the second
As shown in the figure, by inclining the right side of the dust collection chamber starting end wall 27 toward the terminal end side E, the dust collecting chamber starting end wall 27 has a tubular shape more than the end edge 34 of the starting edge 33 in the exhaust gas swirling direction. The opening width S 1 of the dust inlet 9 formed in the space between the starting edge 33 and the terminating edge 34 of the dust collecting chamber starting end wall 27 in the inflow direction of the soot dust 21 is deviated to the starting end side S of the shape body 1. The opening cross-sectional area is widened.

同様の目的は、第3図に示すように、集塵室始端壁27を
螺旋状に形成することにより、集塵室始端壁27の排気ガ
ス旋回方向の始端縁33を終端縁34よりも筒形本体1の始
端側Sに偏位させ、開口幅S2を広げることによっても達
成できる。
As shown in FIG. 3, the same purpose is to form the dust collection chamber starting end wall 27 in a spiral shape so that the dust collecting chamber starting end wall 27 has a starting end edge 33 in the exhaust gas swirling direction more than a trailing end edge 34. This can also be achieved by offsetting the shape body 1 toward the starting end side S and widening the opening width S 2 .

煤塵21が煤塵取出口28付近に集まるようにするため、第
2図の実施例では煤塵21の溜まる集塵室7下部を構成す
る集塵室始端壁27下側を終端側E寄りに位置するように
傾けて集塵室7を下方狭窄状に形成してある。
In order to collect the soot dust 21 in the vicinity of the soot dust outlet 28, in the embodiment shown in FIG. 2, the lower side of the dust collection chamber starting end wall 27 which constitutes the lower part of the dust collection chamber 7 where the soot dust 21 accumulates is located near the end side E. Thus, the dust collection chamber 7 is formed in a downward constricted shape.

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

第1図は本発明の実施例に係る煤塵分離装置を説明する
図で、第1図(A)は一部切欠斜視図、第1図(B)は
縦断面側面図、第1図(C)は第1図(B)のC-C線断
面図である。 第2図と第3図はそれぞれ異なる変更例の要部平面図で
ある。 第4図は従来技術説明図で、第4図(A)は第1図
(A)相当図、第4図(B)は第1図(B)相当図であ
る。 1…筒形本体、S…1の始端側、E…1の終端側、2…
排気ガス入口管、3…排気ガス出口管、4…排気ガス、
5…4の旋回案内板、6…旋回開始室、7…集塵室、8
…7の始端面、9…煤塵入口、10…5の始端部、11…5
の終端部、12…1の軸心、13…5の終端板、14…旋回流
案内筒、15…7の始端内周部、16…煤塵分離筒、17…14
の終端縁、18…16の始端縁、19…18の近傍位置、20…19
よりもE寄りの位置。
FIG. 1 is a diagram for explaining a soot / dust separating apparatus according to an embodiment of the present invention, FIG. 1 (A) is a partially cutaway perspective view, FIG. 1 (B) is a vertical sectional side view, and FIG. ) Is a CC line sectional view of FIG. 1 (B). FIG. 2 and FIG. 3 are plan views of essential parts of different modifications. FIG. 4 is an explanatory view of a conventional technique, FIG. 4 (A) is a view corresponding to FIG. 1 (A), and FIG. 4 (B) is a view corresponding to FIG. 1 (B). 1 ... Cylindrical body, S ... 1 start side, E ... 1 end side, 2 ...
Exhaust gas inlet pipe, 3 ... Exhaust gas outlet pipe, 4 ... Exhaust gas,
5 ... 4 turning guide plate, 6 ... turning start chamber, 7 ... dust collecting chamber, 8
… 7 start end face, 9… dust inlet, 10… 5 start end, 11… 5
End portion, 12 ... 1 axis, 13 ... 5 end plate, 14 ... swirl flow guide tube, 15 ... 7 start end inner peripheral portion, 16 ... soot separation tube, 17 ... 14
End edge of 18… 16 start edge, position near 19… 18, 20… 19
The position closer to E than to.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】筒形本体1内の始端側S中央部に排気ガス
入口管2を、終端側E中央部に排気ガス出口管3を連通
させ、 筒形本体1内の始端側Sの中央部から周囲部に向かって
順に排気ガス4の旋回案内板5と環状の旋回開始室6と
を設け、 筒形本体1内の終端側Eの周囲部に集塵室7を設け、集
塵室7の始端面8に煤塵入口9をあけて構成した、エン
ジンの排気ガス中の煤塵分離装置において、 旋回案内板5の形状を、その始端部10から終端部11に近
づくにつれて筒形本体1の軸心12からの距離が次第に大
きくなる傾斜状に形成した ことを特徴とするエンジンの排気ガス中の煤塵分離装
置。
1. An exhaust gas inlet pipe 2 communicates with a central portion of a starting end side S in a tubular body 1 and an exhaust gas outlet pipe 3 communicates with a central portion of a terminating end side E, and a central portion of the starting end side S in the tubular main body 1 From the portion toward the peripheral portion, a swirl guide plate 5 for the exhaust gas 4 and an annular swirl start chamber 6 are provided in order, and a dust collecting chamber 7 is provided in the peripheral portion on the terminal end side E in the cylindrical main body 1 and the dust collecting chamber is provided. In a soot-dust separating device for exhaust gas from an engine, which is configured by opening a soot-dust inlet 9 on the starting end face 8 of 7, the shape of the swirling guide plate 5 is changed from the starting end 10 to the ending 11 of the tubular body 1. A device for separating dust from engine exhaust gas, characterized by being formed in an inclined shape in which the distance from the shaft center 12 gradually increases.
【請求項2】請求項1に記載のエンジンの排気ガス中の
煤塵分離装置において、 旋回案内板5の終端板13から旋回流案内筒14を終端側E
に向けて突出させ、 集塵室7の始端内周部15から煤塵分離筒16を始端側Sに
向けて突出させ、 旋回流案内筒14の終端縁17を煤塵分離筒16の始端縁18の
近傍位置19乃至これよりも終端側E寄りの位置20に位置
させた ことを特徴とするエンジンの排気ガス中の煤塵分離装
置。
2. The device for separating dust from exhaust gas of an engine according to claim 1, wherein the swirl flow guide cylinder 14 is connected to the end side E from the end plate 13 of the swirl guide plate 5.
Of the dust collection chamber 7 from the inner peripheral portion 15 of the starting end of the dust collecting chamber 7 toward the starting end side S, and the end edge 17 of the swirling flow guiding tube 14 of the starting end edge 18 of the soot dust separating tube 16 A device for separating dust from exhaust gas of an engine, characterized in that the device is located at a position 19 near the position or a position 20 closer to the terminal end E than this.
JP16497290A 1990-06-22 1990-06-22 Device for separating dust from engine exhaust gas Expired - Lifetime JPH0718332B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16497290A JPH0718332B2 (en) 1990-06-22 1990-06-22 Device for separating dust from engine exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16497290A JPH0718332B2 (en) 1990-06-22 1990-06-22 Device for separating dust from engine exhaust gas

Publications (2)

Publication Number Publication Date
JPH0454208A JPH0454208A (en) 1992-02-21
JPH0718332B2 true JPH0718332B2 (en) 1995-03-01

Family

ID=15803384

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16497290A Expired - Lifetime JPH0718332B2 (en) 1990-06-22 1990-06-22 Device for separating dust from engine exhaust gas

Country Status (1)

Country Link
JP (1) JPH0718332B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6227220B2 (en) * 2010-12-27 2017-11-08 Jfeスチール株式会社 Furnace wall shape measuring apparatus, furnace wall shape measuring system, and furnace wall shape measuring method

Also Published As

Publication number Publication date
JPH0454208A (en) 1992-02-21

Similar Documents

Publication Publication Date Title
US4162906A (en) Side outlet tube
US5460147A (en) Cyclone separator for an internal combustion engine
AU2002354406B2 (en) Cyclone separator, liquid collecting box and pressure vessel
EP1205251B1 (en) Cyclonic fluid cleaning apparatus
US5843211A (en) Method and apparatus for separating a heavier phase from a lighter phase in a material flow by centrifugal force
JP4310954B2 (en) Cyclone dust collector
CN112138879B (en) A kind of cyclone separation dust removal method
CN112043202B (en) A cyclone separator and cleaning equipment
CN112169455B (en) Natural gas-liquid separation device, nozzle assembly and application thereof
EP1799353B1 (en) Cyclone collector
CN112122019B (en) Cyclone separation device and cleaning equipment
EP1802399B1 (en) Cyclone collector
JPH08128366A (en) Air cleaner
KR20010018973A (en) structure for inhalation passage of air in multi cyclone dust collector
GB2136326A (en) Improvements in or relating to cyclone separators
US4643158A (en) Vortex particle separator
CN220715151U (en) Cyclone separator and smoking equipment for oil fume separation
JPS63192951A (en) Centrifugal precleaner
CN112439263A (en) Cyclone dust filter
JPH0828281A (en) Engine intake system
CN213133650U (en) Overflow cylinder for cyclone separator
JPH09220421A (en) Swirling gas-liquid separator
JP2001073890A (en) Precleaner
JPH0454208A (en) Device for separating soot in exhaust gas of engine
JPS61153167A (en) Dust collector