JP2595193B2 - Mist removal device - Google Patents
Mist removal deviceInfo
- Publication number
- JP2595193B2 JP2595193B2 JP6048730A JP4873094A JP2595193B2 JP 2595193 B2 JP2595193 B2 JP 2595193B2 JP 6048730 A JP6048730 A JP 6048730A JP 4873094 A JP4873094 A JP 4873094A JP 2595193 B2 JP2595193 B2 JP 2595193B2
- Authority
- JP
- Japan
- Prior art keywords
- mist
- exhaust gas
- inner cylinder
- outer cylinder
- slit
- 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
Links
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- Separating Particles In Gases By Inertia (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は、前段のガス洗浄装置
から排出する排ガス中の煤塵・粉塵が混入したミストを
分離除去して後段の誘引ブロワーの保護をするミスト除
去装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a mist removal device for separating and removing mist mixed with soot and dust in exhaust gas discharged from a gas cleaning device at a preceding stage to protect a suction blower at a later stage.
【0002】[0002]
【従来の技術】ボイラやゴミ焼却炉などの燃焼炉から排
出される排ガスには煤塵や粉塵が含まれ、これらを排ガ
ス中から除去するために一般にはガス洗浄装置が排出系
路内に設けられ、洗浄液あるいは水で洗浄されてフィル
タを通過した後誘引ブロワーにより誘引され外部へ排出
される。2. Description of the Related Art Exhaust gas discharged from a combustion furnace such as a boiler or a refuse incinerator contains soot and dust, and a gas cleaning device is generally provided in the discharge system to remove these from the exhaust gas. After being washed with a washing liquid or water and passing through a filter, the air is attracted by a suction blower and discharged to the outside.
【0003】ガス洗浄装置による洗浄では、排気流れと
直交する方向に設けたグリッド状のフィルタに排ガスを
接触させ排ガス中の洗浄液のミストや煤塵や粉塵を除去
するのが一般的な方法であるが、ミストや煤塵等を完全
に除去することは不可能であり、極微粒子状のものが洗
浄時の水しぶきによる液滴等に含まれてミストとして排
出される。[0003] In the cleaning by a gas cleaning apparatus, it is a general method to contact exhaust gas with a grid-shaped filter provided in a direction orthogonal to the exhaust flow to remove mist, soot and dust of the cleaning liquid in the exhaust gas. However, it is impossible to completely remove mist, dust, and the like, and extremely fine particles are discharged as mist by being included in droplets or the like due to splashes during washing.
【0004】排ガス中の煤塵や粉塵を一次的に分離除去
する手段として、上記ガス洗浄装置以外に例えば実公昭
42−16235号公報のものが知られている。As means for temporarily separating and removing soot and dust in exhaust gas, there is known, for example, Japanese Utility Model Publication No. Sho 42-16235 other than the gas cleaning apparatus.
【0005】この公報による煤煙処理器は、煙突の途中
に挿入して用いられ、下部煙突と同径の接続管の上端を
絞り流速を増したガス流を受入れる翼室で旋回流を生じ
させる遠心力を付与し、漏斗状の旋回室内で旋回流を生
じさせその外周壁に切込みを設けてその舌片を周壁内側
に斜めに押し込んで形成した透孔から煤塵等を一次分離
して除去し、中心側の煤塵の薄いガス流を上部煙突に送
るように形成されている。The soot treatment device according to this publication is used by being inserted in the middle of a chimney, and the upper end of a connecting pipe having the same diameter as the lower chimney is throttled to generate a swirling flow in a blade chamber for receiving a gas flow having an increased flow velocity. By applying force, a swirl flow is generated in the funnel-shaped swirl chamber, cuts are provided in the outer peripheral wall, dust and the like are primarily separated and removed from a through hole formed by obliquely pushing the tongue piece into the inner peripheral wall, It is formed to send a thin gas stream of dust on the center side to the upper chimney.
【0006】[0006]
【発明が解決しようとする課題】ところで、上述した排
ガス中の煤塵、粉塵を一次的に、つまり粗い粉状物、粒
状物を分離除去することは排ガス処理をする場合に重要
であるが、それだけでは極微粒子状の煤塵・粉塵を完全
に分離・除去することはできない。However, it is important to primarily remove soot and dust in the above-mentioned exhaust gas, that is, to separate and remove coarse powder and particulate matter, in the case of exhaust gas treatment. In this case, it is impossible to completely separate and remove ultrafine dust and dust.
【0007】特にガス洗浄装置の場合は、液滴に煤塵・
粉塵を含んだ極微粒子状のミストが残り、これをそのま
ま排出するとブロワーのインペラ等に付着してバランス
が狂い、インペラ等を腐蝕することにより事故の原因と
なる慮れがある。[0007] In particular, in the case of a gas cleaning device, dust droplets
Ultrafine mist containing dust remains, and if the mist is discharged as it is, it adheres to the impeller or the like of the blower, causing imbalance and corroding the impeller or the like, which may cause an accident.
【0008】又、性能にも悪影響を及ぼし、誘引ブロワ
ーの正常な長時間連続運転が困難となることもあり、煤
塵、粉塵を含む極微粒子状のミストをさらに二次分離し
て除去する必要がある。[0008] In addition, the performance may be adversely affected, and it may be difficult to operate the induction blower normally for a long period of time. Therefore, it is necessary to further secondary-separate and remove ultra-fine mist including dust and dust. is there.
【0009】そこで上記目的に沿う二次分離・除去手段
として、特開昭62−213819号によるミスト除去
装置が既に提案されている。このミスト除去装置は、上
部に小口径の吐出円筒部を有し、下部ガス流入側の中央
部に案内羽根を設けたドラムを装備した円筒形の主体
と、この主体の外周囲に、この主体に設けた窓孔を介し
て主体内と連通する捕集管を配備したものとして構成さ
れている。Therefore, as a secondary separation / removal means to meet the above-mentioned object, a mist removal apparatus disclosed in Japanese Patent Application Laid-Open No. 62-13819 has already been proposed. This mist removing device has a cylindrical main body equipped with a drum having a small-diameter discharge cylindrical part in the upper part and a guide blade provided in the center part on the lower gas inflow side, and an outer periphery of the main body, And a collecting pipe communicating with the inside of the main body through the window hole provided in the main body.
【0010】上記先の出願によるミスト除去装置は、主
体の外周囲の捕集管に連通するための窓孔の内側に突起
物を一切排除し、案内羽根を有するドラムにより排ガス
流れに生じた遠心力でミストを分離し、かつ窓孔付近に
乱流を生じないようにしてミストの分離・除去作用を確
実に得られるようにした点で優れた効果を有している。The mist removing device according to the above-mentioned application eliminates any projection inside a window hole for communicating with a collecting pipe around the outside of the main body, and a centrifugal gas generated in an exhaust gas flow by a drum having guide vanes. It has an excellent effect in that the mist is separated by force and turbulence is not generated in the vicinity of the window hole so that the action of separating and removing the mist can be reliably obtained.
【0011】しかしながら、上記ミスト除去装置では、
排ガス流れに遠心分離作用を与えるための案内羽根を有
するドラムは案内羽根が主体内径と平行な面上に設けら
れているため遠心力による分離作用を大きくするには限
界がある。However, in the above mist removing device,
A drum having guide vanes for imparting a centrifugal separation effect to the exhaust gas flow has a limit in increasing the separation effect by centrifugal force because the guide vanes are provided on a surface parallel to the main body inner diameter.
【0012】又、ドラム後方で旋回動している排ガスを
中心側に集めて吐出管から吐出するように構成されてい
るため、主体内部のわずかな変動要因で旋回流れに乱れ
が生じると中心側と外側の排ガスが混合してミストの分
離効率が低下するという問題がある。Further, since exhaust gas orbiting behind the drum is collected at the center side and discharged from the discharge pipe, if a turbulence occurs in the swirling flow due to a slight fluctuation factor inside the main body, the center side is exhausted. There is a problem that the mist separation efficiency is reduced due to mixing of the mist with the outside exhaust gas.
【0013】この発明は、上述した従来のミスト除去装
置の問題点に留意して、簡易な構成でかつ経済的なコス
トで大きな遠心力による分離・除去作用の得られるミス
ト除去装置を得ることを課題とする。The present invention has been made in consideration of the above-mentioned problems of the conventional mist removing device, and has an object to obtain a mist removing device having a simple structure and economical cost and capable of performing a separating / removing action by a large centrifugal force. Make it an issue.
【0014】[0014]
【課題を解決するための手段】上記課題を解決する手段
としてこの発明は、外筒とその内側に同心円状に設けた
内筒を備え、外筒の一端を排ガスが流入する開口とし、
その入口開口に臨む円錐面に沿って適宜間隔で案内羽根
を有する円錐体を内筒端に設け、円錐体より下流側の両
円筒間スペースを上記案内羽根で旋回しながら流れる排
ガスからミストを分離する分離領域とし、この分離領域
に対応する外筒壁にミストを排出するためのスリットを
排ガスの流れに対し傾斜状にかつ互いに略平行で上下多
段状に設けると共に上記スペース下端を閉じ、内筒壁に
はミストを除去された排ガスを受入れる開口を設けかつ
内筒下流端を排ガスの排出口として成るミスト除去装置
としたのである。As a means for solving the above problems, the present invention comprises an outer cylinder and an inner cylinder provided concentrically inside the outer cylinder, one end of the outer cylinder being an opening through which exhaust gas flows,
Cones having guide vanes at appropriate intervals along the conical surface facing the inlet opening are provided at the end of the inner cylinder, and mist is separated from exhaust gas flowing while turning the space between both cylinders downstream of the cone with the guide vanes. A slit for discharging mist is formed on the outer cylinder wall corresponding to this separation area.
Vertically and obliquely to the flow of exhaust gas and substantially parallel to each other
The mist removing device is provided in a stepped manner, the lower end of the space is closed, an opening for receiving exhaust gas from which mist has been removed is provided in the inner cylinder wall, and the downstream end of the inner cylinder is used as an exhaust gas outlet.
【0015】この場合好ましい態様として、前記円錐体
の基部径を内筒径より大としたものとすることができ
る。[0015] As this preferred embodiment, it can be those larger than the inner cylinder diameter base diameter before Kien cone.
【0016】さらに別の態様として、前記各スリットは
細曲線状の連通スリットとし、このスリットから排出さ
れたミストを捕集する捕集管を外筒外側に設けると共に
捕集管に外気との連通を遮断する排出部を設けてミスト
を除去するのが好ましい。[0016] In yet another embodiment, prior to SL and the communicating slit of each slit narrow curved, outside air of the collecting pipe provided with a collecting tube for collecting the mist that is discharged from the slit in the outer tube outwardly It is preferable to provide a discharge section for interrupting communication to remove mist.
【0017】[0017]
【作用】上記の構成とした第一の発明のミスト除去装置
は、この装置の後方に設けられる誘引ブロワーにより排
ガスが吸引されて入口開口から流入するように使用する
のを前提とする。排ガスはボイラ等の燃焼炉から排出さ
れ、排ガス中には煤塵、粉塵が含まれている。The mist removing device according to the first aspect of the present invention is configured so that exhaust gas is sucked by an induction blower provided at the rear of the device and is used so as to flow through an inlet opening. The exhaust gas is discharged from a combustion furnace such as a boiler, and the exhaust gas contains soot and dust.
【0018】入口開口から流入する排ガスは円錐体の表
面に設けられた案内羽根により円周方向に送られ旋回動
しながら外筒の内壁と円錐体基部との間を通り分離領域
へ流入する。この分離領域でさらに旋回動する間に排ガ
ス中に含まれる煤塵や粉塵を含む質量の重い液状のミス
トは遠心力により外筒内壁へ達して外筒に設けたスリッ
トから外部へ排出される。Exhaust gas flowing from the inlet opening is sent in the circumferential direction by guide vanes provided on the surface of the cone and, while rotating, flows between the inner wall of the outer cylinder and the base of the cone into the separation region. While further turning in this separation region, the heavy liquid mist containing soot and dust contained in the exhaust gas reaches the inner wall of the outer cylinder by centrifugal force and is discharged to the outside through a slit provided in the outer cylinder.
【0019】上記ミストを遠心分離する際に、排ガスは
内筒と外筒の間の狭い厚みのドーナツ状スペースから成
る分離領域でミストの遠心分離が行なわれる。従って、
内筒側に拡散した排ガス中のミストであっても外筒内壁
までの飛距離が短いため容易に外筒内壁へ達する。When the mist is centrifuged, the mist of the exhaust gas is centrifuged in a separation region consisting of a narrow donut-shaped space between the inner cylinder and the outer cylinder. Therefore,
Even the mist in the exhaust gas diffused to the inner cylinder side easily reaches the outer cylinder inner wall because the flight distance to the outer cylinder inner wall is short.
【0020】こうして分離除去されたミストは、スリッ
トから外部へ排出され、ミストを分離除去された排ガス
はクリーンなガスとして内筒下方の排出口から排出され
る。The mist thus separated and removed is discharged to the outside through the slit, and the exhaust gas from which the mist is separated and removed is discharged as a clean gas from an outlet below the inner cylinder.
【0021】第二の発明の装置では、円錐体基部径を内
筒径より大としており、この場合は入口開口から流入す
る排ガスは大きな旋回動をして円錐体基部から分離領域
へ流入する。このため、遠心分離作用が大きく、ミスト
の捕集効率が最大となる。[0021] In apparatus of the second invention, has been larger than the inner cylinder diameter circular cone base diameter, in this case, exhaust gas flowing from the inlet opening flows from cone base and a large pivotal movement to the separation region . For this reason, the centrifugal separation action is large, and the mist collection efficiency is maximized.
【0022】第三の発明では、スリットを多段の細曲線
状連通状スリットとし、スリットが排出されるミストの
捕集管を外筒の外側に設けこの捕集管の排出部で外気と
の連通を遮断するようにしている。In the third aspect of the invention, the slit is formed as a multi-step finely curved communication slit, and a mist collection pipe for discharging the slit is provided outside the outer cylinder, and the discharge section of the collection pipe communicates with the outside air. I try to cut off.
【0023】このため、スリットを介して外気が分離領
域に流入しないようになり、分離領域に乱流が生じるの
が防止され、かつ吸引力よりも遠心力による分離・除去
作用の方が大きいためミストは吸引力で内筒側へ吸引さ
れることなく効率よく分離・除去され捕集される。For this reason, outside air does not flow into the separation area through the slit, and turbulence is prevented from being generated in the separation area, and the separation / removal action by the centrifugal force is larger than the suction force. The mist is efficiently separated / removed and collected without being sucked toward the inner cylinder by the suction force.
【0024】[0024]
【実施例】以下この発明の実施例について図面を参照し
て説明する。図1は実施例のミスト除去装置の概略斜視
図、図2はその主要断面図である。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic perspective view of a mist removing device according to an embodiment, and FIG. 2 is a main sectional view thereof.
【0025】外筒1の内側には同心円状の内筒が設けら
れ、外筒1の一端は径が絞られ入口管3が接続されてい
る。入口管3は、上流でガス洗浄装置(図示省略)によ
り粒径の大きい煤塵、粉塵等が除去された後の液滴に極
微粒子状の煤塵、粉塵を含むミストの混合した排ガスが
流れる排気管(図示省略)に接続されるものであり、一
般には排気管と同径である。A concentric inner cylinder is provided inside the outer cylinder 1. One end of the outer cylinder 1 has a reduced diameter and an inlet pipe 3 is connected thereto. The inlet pipe 3 is an exhaust pipe through which exhaust gas in which ultrafine particulate dust and mist containing dust are mixed into droplets after dust and dust having a large particle diameter are removed by a gas cleaning device (not shown) upstream. (Not shown), which is generally the same diameter as the exhaust pipe.
【0026】上記外筒1の入口管3から少し中に入った
位置には上記入口管3に円錐面を臨ませて設けられた円
錐ドラム4が内筒2の同じ側端に固定され、内筒2の上
端を密閉している。円錐ドラム4は、図示のように、断
面が丁度そろばん玉のような形状で、円錐ドラム基部
(直径が最大の部分)の径が内筒2の径より大きく形成
されている。円錐ドラム4の円錐面には、図3の断面に
示すように、適当な間隔で円錐面に沿って案内羽根5が
略螺旋状の一部をなすように立設されている。At a position slightly inside the outer tube 1 from the inlet tube 3, a conical drum 4 provided with the conical surface facing the inlet tube 3 is fixed to the same side end of the inner tube 2. The upper end of the cylinder 2 is sealed. As shown in the drawing, the conical drum 4 has a cross section just like an abacus ball, and the diameter of the conical drum base (the portion having the largest diameter) is larger than the diameter of the inner cylinder 2. On the conical surface of the conical drum 4, as shown in the cross section of FIG. 3, guide blades 5 are provided upright at appropriate intervals along the conical surface so as to form a substantially spiral part.
【0027】上記円錐ドラム4より下流側の内、外筒間
スペースは、図示のAを分離領域とし、ここで排ガス中
のミストが分離除去される。この分離領域の内筒壁には
排ガスを受入れるための内筒開口6が所定間隔で設けら
れ、外筒壁にはスリット7がこれも所定の間隔で設けら
れている。The space between the outer cylinders on the downstream side of the conical drum 4 is designated by A as a separation region, where mist in the exhaust gas is separated and removed. Inner cylinder openings 6 for receiving exhaust gas are provided at predetermined intervals on the inner cylinder wall of the separation area, and slits 7 are also provided at predetermined intervals on the outer cylinder wall.
【0028】スリット7が設けられている外筒壁外側に
は捕集管8が設けられ、スリット7より下方の適当な位
置でこれら捕集管8からのミストを集めるための捕集連
絡管8aが外筒の外周に設けられ、その適宜位置にはS
字トラップ9aを含むドレン管9が接続されている。A collecting pipe 8 is provided outside the outer cylinder wall where the slit 7 is provided, and a collecting connecting pipe 8a for collecting mist from the collecting pipe 8 at an appropriate position below the slit 7. Is provided on the outer periphery of the outer cylinder, and S
A drain pipe 9 including a character trap 9a is connected.
【0029】上記分離領域Aを形成する内、外筒間のス
ペースの下方は盲板1aで閉じられている。又、内筒2
の下流側は内筒吐出部10として開放され、さらに下流
側の排気管(図示省略)に接続し得るように形成されて
いる。11は盲板1aで閉じられた部分にたまるドレン
の排出孔で適宜位置に複数個設けられている。In the separation area A, the lower part of the space between the outer cylinders is closed by a blind plate 1a. Also, inner cylinder 2
The downstream side is opened as an inner cylinder discharge part 10 and is formed so as to be connectable to a downstream exhaust pipe (not shown). A plurality of drain holes 11 are provided at appropriate positions, and the drain holes collect in a portion closed by the blind plate 1a.
【0030】図4に、図2の矢印IV−IVから見たスリッ
ト7の部分拡大図を示す。図示のように、スリット7は
細曲線状の連通スリット7を上下多段状に、かつ外筒1
の内周壁に沿って旋回移動する排ガス流れに大略沿う方
向に斜めに傾けて設けられている。連通スリット7a
は、例えばこの実施例では幅5mm、曲率半径が70mm、
円弧の長さは約40°程度の細曲線状のものとしてい
る。これはあくまで一例であり、これに限定されるもの
ではない。[0030] FIG. 4 shows a partially enlarged view of the slit 7 as viewed from an arrow IV-IV of FIG. As shown in the drawing, the slit 7 is formed by connecting the communication slit 7 having a fine curved shape in a multi-stage manner in the upper and lower directions and the outer cylinder 1.
It is provided obliquely in a direction substantially along the flow of the exhaust gas that swirls along the inner peripheral wall of the airbag. Communication slit 7a
For example, in this embodiment, the width is 5 mm, the radius of curvature is 70 mm,
The length of the arc is a fine curve of about 40 °. This is only an example, and the present invention is not limited to this.
【0031】上記のような構成とした実施例のミスト除
去装置では次のようにミスト除去が行なわれる。In the mist removing device of the embodiment having the above-described structure, mist is removed as follows.
【0032】上流のガス洗浄装置から送られてくる極微
粒子状の煤塵、粉塵を含むミストの混入した排ガスが入
口管3から垂直に流入すると、円錐ドラム4によって円
の中心から外向きに広がりながら、案内羽根5に案内さ
れて円運動をして円錐ドラム4の下流の分離領域Aへと
進み、分離領域A内で螺旋状に流れる。When the exhaust gas containing mist containing fine particulates and dust sent from the upstream gas cleaning device flows vertically from the inlet pipe 3, the conical drum 4 spreads outward from the center of the circle outward. Is guided by the guide vanes 5 and moves in a circular motion to the separation area A downstream of the conical drum 4 and flows spirally in the separation area A.
【0033】上記円錐ドラム4の案内羽根5で円運動す
る際に、円錐ドラム4の基部(径の最大部)の径は内筒
2の径よりも大きく、例えば図示の例では内筒2と外筒
1の中間程度としているから、排ガスは上記基部と外筒
1の内壁間の隙間を通って、しかも螺旋運動しながら通
過するため排ガスの大部分に外方向の慣性力と遠心力が
同時に作用する。When the guide blade 5 of the conical drum 4 makes a circular motion, the diameter of the base (the largest part of the diameter) of the conical drum 4 is larger than the diameter of the inner cylinder 2. Since the exhaust gas passes through the gap between the base portion and the inner wall of the outer cylinder 1 while passing through the outer cylinder 1 while being spirally moved, the inertia force and the centrifugal force in the outer direction are simultaneously applied to most of the exhaust gas. Works.
【0034】上記慣性力と遠心力を受けた排ガスは、上
記隙間を通過後も螺旋運動しながら遠心力が引続き作用
した状態で進むため比重の大きいミストは大部分外筒の
内壁に沿って進む。一方、上記隙間を通過した排ガス
は、円錐ドラム4の基部より下流側では内筒2の径が小
さいため通過スペースが拡大し、このため排ガスの一部
が内側に拡散する。The exhaust gas which has received the above inertial force and centrifugal force travels in a state where the centrifugal force continues to act while spirally moving even after passing through the gap, so that the mist having a large specific gravity mostly travels along the inner wall of the outer cylinder. . On the other hand, the exhaust gas that has passed through the gap has a smaller passage diameter because the diameter of the inner cylinder 2 is smaller on the downstream side than the base of the conical drum 4, so that a part of the exhaust gas diffuses inward.
【0035】しかし、排ガスが一部内側に拡散しても全
体としてはなお旋回流となっているため分離領域Aでも
引き続き比重の大きいミストはスペースの外側、即ち外
筒1の内壁へと移動させられるのである。この場合、円
錐ドラム4基部から外筒1の内壁までの飛距離は極めて
小さく、排ガスの一部が内側に拡散した場合でも外筒1
の内壁までの飛距離はそれ程大きくないため、容易にミ
ストは外筒1の内壁に到達できる。However, even if the exhaust gas partially diffuses inward, the mist still having a large specific gravity continues to move to the outside of the space, that is, to the inner wall of the outer cylinder 1 even in the separation region A because the swirl flow still remains as a whole. It is done. In this case, the flight distance from the base of the conical drum 4 to the inner wall of the outer cylinder 1 is extremely small, and even if a part of the exhaust gas diffuses inward, the outer cylinder 1
The mist can easily reach the inner wall of the outer cylinder 1 because the flight distance to the inner wall is not so large.
【0036】ちなみに、従来の一次分離を行なう煤煙処
理器などでは、この実施例のように分離領域Aに内筒2
に相当する部材が設けられておらず、この実施例の円錐
ドラム4と案内羽根5に相当する部分を通過した直後
に、直進する排ガスとその一部が円運動して遠心分離に
より煤塵・粉塵を分離した排ガスとが再び下流域で混合
するため、中心側に移動した比重の大きいミストを旋回
させても外周壁までの距離が大きくて外周壁へ到達でき
ないのである。By the way, in a conventional soot treatment device or the like for performing primary separation, the inner cylinder 2 is placed in the separation region A as in this embodiment.
Is not provided, and immediately after passing through the portion corresponding to the conical drum 4 and the guide blade 5 of this embodiment, the exhaust gas that goes straight and a part thereof moves in a circular motion, and the dust and the dust are separated by centrifugal separation. Is mixed again in the downstream region, so that even if the mist moved to the center side and having a large specific gravity is swirled, the distance to the outer peripheral wall is too large to reach the outer peripheral wall.
【0037】以上のように排ガス流れが旋回流となって
分離領域Aを下降する間に排ガス中から分離・除去され
た大部分のミストは外筒1の内周壁に到達するが、この
内周壁には適宜間隔でスリット7が設けられており、こ
のスリット7を通過して上記ミストは外筒1の外へ排出
される。As described above, most of the mist separated and removed from the exhaust gas reaches the inner peripheral wall of the outer cylinder 1 while the exhaust gas flow is swirling and descends the separation area A. Are provided with slits 7 at appropriate intervals, and the mist is discharged outside the outer cylinder 1 through the slits 7.
【0038】上記スリット7は、排ガスの旋回流の流れ
に沿って細曲線状に形成した連通スリット7aを上下多
段状に設けて成る。これは、外筒1の内周面に幅の広い
スリットを設けると内周壁に到達したミストを含む排ガ
ス流れに乱流が生じる慮れがあり、これを防止するため
である。The slit 7 is provided with a communication slit 7a formed in a fine curve along the swirl flow of the exhaust gas in a multi-tiered manner. This is because if a wide slit is provided on the inner peripheral surface of the outer cylinder 1, there is a possibility that turbulent flow may occur in the exhaust gas flow including the mist that has reached the inner peripheral wall, and this is prevented.
【0039】連通スリット7aは、本来は点状の小孔で
あるのが望ましいが、これを多数連続状に設けるのは現
実的でない。このため、この実施例のスリット7は多数
の小孔を互いに連通して細曲線状としているのである。The communication slit 7a is originally desirably a point-like small hole, but it is not realistic to provide many continuous slits. For this reason, the slit 7 of this embodiment has a number of small holes communicating with each other to form a fine curve.
【0040】上記スリット7から排出されたミストは、
相互に接触、粗大化しながら捕集管8を通り捕集連絡管
8aで集められてドレン管9から排出され、例えば外部
に設置れる貯槽(図示省略)に至る。このとき、ドレン
管9の途中にはS字トラップ9aが設けられ、そこに封
入された液部で捕集管8の内部は外気と遮断されてい
る。The mist discharged from the slit 7 is
While contacting and coarsening with each other, they are collected by the collection communication pipe 8a through the collection pipe 8 and discharged from the drain pipe 9 to reach, for example, an external storage tank (not shown). At this time, an S-shaped trap 9a is provided in the middle of the drain tube 9, and the inside of the collection tube 8 is shut off from the outside air by the liquid part sealed therein.
【0041】このため、内筒2の下方の内筒吐出部10
の後方に接続される誘引ブロワーからの吸引力が作用し
ても、その吸引力でドレン管9から外気を直接吸引しな
いようにして排ガス流れが乱流になるのが防止される。
又、上記吸引力が作用しても、分離領域Aで分離・除去
されるミストは旋回速度と遠心力により半径方向へ押し
出す作用の方が吸引力以上となるようにすれば吸引力で
分離・除去作用を阻害されることはない。For this reason, the inner cylinder discharge portion 10 below the inner cylinder 2
Even if a suction force is applied from an induction blower connected to the rear of the exhaust pipe, the suction force does not directly suck the outside air from the drain pipe 9 to prevent the exhaust gas flow from becoming turbulent.
Even if the above-mentioned suction force acts, the mist separated and removed in the separation area A is extruded in the radial direction by the swirling speed and the centrifugal force so that the action is more than the suction force. The removal action is not inhibited.
【0042】従って、上記スリット7は排ガス流れが旋
回速度と遠心力の関係から流体の架橋を維持できる、即
ち連続流れを阻害しないように維持し得る最大限の連通
孔とするのが望ましい。このため、スリット7は細い曲
線状の連通スリットとしたのであり、このスリット7は
図4に示すように、排ガス流れの方向に流れの幅を網羅
し得る配置としている。Accordingly, it is desirable that the slit 7 be a communication hole which can maintain the cross-linking of the fluid in the exhaust gas flow in view of the relationship between the swirling speed and the centrifugal force, that is, can maintain the flow so as not to hinder the continuous flow. For this reason, the slit 7 is a thin curved communication slit, and as shown in FIG. 4, the slit 7 is arranged so as to cover the width of the exhaust gas in the direction of the exhaust gas flow.
【0043】上記スリット7を設けた外筒1の内周壁表
面付近では、スリット7を設けたために旋回流にわずか
な乱流が生じる可能性があるが、排ガス流れがスリット
面を通過後直ちに旋回流は遠心力によって修復されて流
体に乱流が生じたままとなるのは回避できる。即ち、図
4および図5に示すように、スリット7での旋回流の流
体圧(面圧)があまり大きな面積でかからない幅および
長さで落込み・起伏が生じるようにして乱流の影響を防
止するのである。詳細には、図4の如く、落込み・起伏
が所定の幅(スリット7の幅)で順次右方向へ行われ
る。換言すれば、流れ方向の垂直角に位置する流体は小
さな面積で落込み・起伏が時間差をもって行われる。こ
れによって乱流は最小限になる。尚、スリット7を多段
設けると全高(分離領域)を網羅することができる。Near the inner peripheral wall surface of the outer cylinder 1 provided with the slit 7, there is a possibility that a slight turbulence may occur in the swirl flow due to the provision of the slit 7, but the exhaust gas flow swirls immediately after passing through the slit surface. The flow can be prevented from being restored by centrifugal force and leaving the fluid turbulent. That is, as shown in FIGS. 4 and 5, the fluid pressure (surface pressure) of the swirling flow at the slit 7 causes a drop and undulation at a width and a length which are not applied to a very large area, thereby reducing the influence of the turbulent flow. Prevent it. More specifically, as shown in FIG. 4, the drop and the undulation are sequentially performed to the right at a predetermined width (the width of the slit 7). In other words, the fluid located at a vertical angle in the flow direction falls and undulates in a small area with a time difference. This minimizes turbulence. If the slits 7 are provided in multiple stages, the entire height (separation region) can be covered.
【0044】さらに、排ガス流れのミストに粉体(個体
状)が混入していても、液状のミストにより連通スリッ
トの面は絶えず洗浄されるから、スリットが目詰りする
ことがなく、長時間連続運転しても捕集効率、圧力損失
の変動が生じないのである。Furthermore, even if powder (solid state) is mixed in the mist of the exhaust gas flow, the surface of the communicating slit is constantly washed by the liquid mist, so that the slit is not clogged and continuous for a long time. There is no fluctuation in the collection efficiency and pressure loss even when the operation is performed.
【0045】こうして、ほぼ完全にミストを分離・除去
された排ガスは、誘引ブロワーにより吸引されて内筒吐
出部10から排出され、排ガスはクリーンな状態である
ため誘引ブロワー等が汚れないで済むこととなる。The exhaust gas from which the mist has been almost completely separated and removed is sucked by the induction blower and discharged from the inner cylinder discharge section 10. Since the exhaust gas is in a clean state, the induction blower and the like need not be contaminated. Becomes
【0046】なお、上記実施例では外筒1の排ガスの入
口開口となる入口管3は内筒径よりも若干小さい例を示
しているが、この入口開口は必ずしも内筒径より小さく
なくてもよく、例えば外筒1の最大径部と同じであって
もよく、その中間の任意の径としてもよい。In the above embodiment, the inlet pipe 3 serving as the exhaust gas inlet opening of the outer cylinder 1 is slightly smaller than the inner cylinder diameter. However, the inlet opening is not necessarily smaller than the inner cylinder diameter. For example, it may be the same as the maximum diameter portion of the outer cylinder 1, or may be an arbitrary diameter in the middle.
【0047】その場合は、上記実施例のように入口管3
から案内羽根5により旋回動が与えられる際の遠心力が
若干減少するが、吸引力や案内羽根の角度、あるいは円
錐ドラムの径、円錐率などを調整することによって最大
限の遠心力を得るようにすればよい。In such a case, as in the above embodiment, the inlet pipe 3
Although the centrifugal force when the swiveling motion is given by the guide blade 5 slightly decreases, the maximum centrifugal force can be obtained by adjusting the suction force, the angle of the guide blade, the diameter of the conical drum, the conical ratio, and the like. What should I do?
【0048】[0048]
【効果】以上詳細に説明したように、この出願の第一の
発明のミスト除去装置は、外筒内に設けた内筒の端に案
内羽根を有する円錐ドラムを設け、外筒端の入口開口か
ら流入する排ガスの円運動による遠心分離作用で排ガス
からミストを分離除去してクリーンな排ガスを排出する
ようにしたから、シンプルな構成で経済的なコストで製
造ができ、排気管導中に挿入自在であるために設置が容
易であり、かつミストを分離・除去する捕集効率の極め
て高いミスト除去装置が得られるという利点がある。As described in detail above, the mist removing device of the first invention of this application has a conical drum having guide vanes at the end of an inner cylinder provided in an outer cylinder, and has an inlet opening at the end of the outer cylinder. The mist is separated and removed from the exhaust gas by the centrifugal action of the exhaust gas flowing in from the cylinder to discharge clean exhaust gas, so it can be manufactured with a simple configuration at economical cost and inserted into the exhaust pipe. Since it is free, installation is easy, and there is an advantage that a mist removing device with extremely high collection efficiency for separating and removing mist can be obtained.
【0049】第二の発明では、円錐体基部径を内筒径よ
り大としたから、排ガスに大きな遠心力が作用し、遠心
力でミストを分離除去する位置から外筒内壁までの飛距
離が小さくなって極めて高い捕集効率でミストが分離除
去される。[0049] In the second invention, distance of from were larger than the inner cylinder diameter circular cone base diameter, large centrifugal force to the exhaust gas acts, from a position separated off mist by centrifugal force to the outer tube inner wall And the mist is separated and removed with extremely high collection efficiency.
【0050】第三の発明では、スリットを多段状の連通
スリットとし、スリットから排出されたミストを捕集す
る捕集管に設けた排出部により外気との連通を遮断した
から、スリットを設けることにより分離領域が外気に連
通することなく排出ガスが吸引され、従って外筒内の分
離領域に乱流を生ずることなく確実にミストの分離・除
去作用を得ることができるという利点が得られる。In the third invention, the slit is formed as a multi-stage communication slit, and communication with the outside air is interrupted by a discharge portion provided in a collection tube for collecting the mist discharged from the slit. Accordingly, an advantage is obtained that the exhaust gas is sucked without the separation region communicating with the outside air, so that the mist separation / removal operation can be surely obtained without generating a turbulent flow in the separation region in the outer cylinder.
【図面の簡単な説明】[Brief description of the drawings]
【図1】実施例のミスト除去装置の外観斜視図FIG. 1 is an external perspective view of a mist removing device according to an embodiment.
【図2】同上の主要断面図FIG. 2 is a main sectional view of the above.
【図3】図2の矢印III −III から見た断面図FIG. 3 is a sectional view taken along arrow III-III in FIG. 2;
【図4】図2の矢印IV−IVから見た拡大図FIG. 4 is an enlarged view as viewed from arrows IV-IV in FIG. 2;
【図5】作用の説明図FIG. 5 is an explanatory diagram of an operation.
1 外筒 2 内筒 3 入口管 4 円錐ドラム 5 案内羽根 6 内筒開口部 7 スリット 8 捕集管 9 ドレン管 10 内筒吐出部 DESCRIPTION OF SYMBOLS 1 Outer cylinder 2 Inner cylinder 3 Inlet pipe 4 Conical drum 5 Guide vane 6 Inner cylinder opening 7 Slit 8 Collection pipe 9 Drain pipe 10 Inner cylinder discharge part
Claims (3)
を備え、外筒の一端を排ガスが流入する開口とし、その
入口開口に臨む円錐面に沿って適宜間隔で案内羽根を有
する円錐体を内筒端に設け、円錐体より下流側の両円筒
間スペースを上記案内羽根で旋回しながら流れる排ガス
からミストを分離する分離領域とし、この分離領域に対
応する外筒壁にミストを排出するためのスリットを排ガ
スの流れに対し傾斜状にかつ互いに略平行で上下多段状
に設けると共に上記スペース下端を閉じ、内筒壁にはミ
ストを除去された排ガスを受入れる開口を設けかつ内筒
下流端を排ガスの排出口として成るミスト除去装置。1. An outer cylinder and an inner cylinder provided concentrically inside the outer cylinder. One end of the outer cylinder is an opening through which exhaust gas flows, and guide blades are provided at appropriate intervals along a conical surface facing the inlet opening. A conical body is provided at the end of the inner cylinder, and a space between the two cylinders downstream of the conical body is used as a separation area for separating mist from exhaust gas flowing while rotating with the guide vanes, and mist is formed on the outer cylinder wall corresponding to the separation area. Discharge slit for discharging
Up and down multi-stage with slanted shape and almost parallel to each other
A mist removing device, wherein the lower end of the space is closed, the inner cylinder wall is provided with an opening for receiving the exhaust gas from which the mist has been removed, and the downstream end of the inner cylinder is used as the exhaust gas discharge port.
たことを特徴とする請求項1に記載のミスト除去装置。2. A mist removing apparatus according to claim 1, characterized in that a larger than the inner cylinder diameter base diameter before Kien cone.
トとし、このスリットから排出されたミストを捕集する
捕集管を外筒外側に設けると共に捕集管に外気との連通
を遮断する排出部を設けてミストを除去することを特徴
とする請求項1又は2に記載のミスト除去装置。3. Before SL slits and thin curved communicating slits, cuts off the communication between the outside air collecting tube for collecting the mist that is discharged from the slits to the collecting tube with an outer tube provided on the outer The mist removing device according to claim 1 or 2, wherein a mist is removed by providing a discharge unit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6048730A JP2595193B2 (en) | 1994-03-18 | 1994-03-18 | Mist removal device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6048730A JP2595193B2 (en) | 1994-03-18 | 1994-03-18 | Mist removal device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07256030A JPH07256030A (en) | 1995-10-09 |
JP2595193B2 true JP2595193B2 (en) | 1997-03-26 |
Family
ID=12811415
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6048730A Expired - Lifetime JP2595193B2 (en) | 1994-03-18 | 1994-03-18 | Mist removal device |
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Country | Link |
---|---|
JP (1) | JP2595193B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005095859A1 (en) * | 2004-03-30 | 2005-10-13 | Park, Young Woo | Combustion gas cleaning apparatus |
CN103084010A (en) * | 2011-11-02 | 2013-05-08 | 上海远跃制药机械股份有限公司 | Concentrator foam collecting device |
CN105169818B (en) * | 2015-07-27 | 2017-01-11 | 航天环境工程有限公司 | Double-vane air-swirl parallel-combination demister and application thereof |
CN108355404B (en) * | 2018-04-13 | 2023-12-26 | 苏州中新动力科技股份有限公司 | High-temperature corrosion resistant power defogging device |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5799717U (en) * | 1980-12-11 | 1982-06-19 | ||
JP3032918U (en) * | 1996-04-16 | 1997-01-17 | 芳郎 中野 | Cutting device for sealed pieces in filling device |
-
1994
- 1994-03-18 JP JP6048730A patent/JP2595193B2/en not_active Expired - Lifetime
Also Published As
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JPH07256030A (en) | 1995-10-09 |
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