JPS62213819A - Mist removal device - Google Patents
Mist removal deviceInfo
- Publication number
- JPS62213819A JPS62213819A JP5768886A JP5768886A JPS62213819A JP S62213819 A JPS62213819 A JP S62213819A JP 5768886 A JP5768886 A JP 5768886A JP 5768886 A JP5768886 A JP 5768886A JP S62213819 A JPS62213819 A JP S62213819A
- Authority
- JP
- Japan
- Prior art keywords
- main body
- drum
- exhaust gas
- mist
- collecting tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000003595 mist Substances 0.000 title claims abstract description 24
- 238000000034 method Methods 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 25
- 238000006477 desulfuration reaction Methods 0.000 description 4
- 230000023556 desulfurization Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000002093 peripheral effect Effects 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 241000207199 Citrus Species 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 235000020971 citrus fruits Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、燃焼排気ガスの脱硫装置等による洗浄の際
に発生する酸性の霧滴(ミスト)を遠心作用lこより分
離捕集するミスト除去装置に関する。Detailed Description of the Invention [Industrial Application Field] This invention is a mist removal method that separates and collects acidic mist droplets (mist) generated when cleaning combustion exhaust gas by a desulfurization device, etc. using a centrifugal action. Regarding equipment.
従来、上記脱硫装置等により発生する酸性の霧滴を除去
する方法として、排気ガスの流量が太きい場合はその排
気管中に流れと直交する方向lこグリッド状のフィルタ
ーを設け、このフィルターにおいて霧滴を接触、衝突せ
しめることによってミスト除去を行なっていた。又、流
量が小さいときは、気体サイクロン装置lこよって除去
することも可能である。Conventionally, as a method for removing acidic mist droplets generated by the above-mentioned desulfurization equipment, etc., when the flow rate of exhaust gas is large, a grid-shaped filter is installed in the exhaust pipe in a direction perpendicular to the flow. Mist removal was performed by bringing mist droplets into contact and colliding with each other. Moreover, when the flow rate is small, it is also possible to remove it using a gas cyclone device.
しかしながら、排気ガス中Fこ含まれる微細な霧滴は、
フィルターの#!回の大きさよりはるかlこ微小であり
、このフィルターで除去し得る霧滴は限られたものであ
る。また気体サイクロン装置は、装置本体に流入するガ
スを本体に対して接線方向に吹込む形式上、流量に制約
を受け、大流量の排気ガスのミスト除去に適さないとい
う難点がある。However, the fine mist droplets contained in the exhaust gas,
# of filters! The size of the mist is much smaller than that of the air, and the number of mist droplets that can be removed by this filter is limited. Further, the gas cyclone device has a drawback in that it is not suitable for removing mist from a large flow rate of exhaust gas because the gas flowing into the main body of the device is blown in in a tangential direction to the main body, so the flow rate is restricted.
この発明は、上記問題点に鑑みてなされたものであり、
その目的は固定案内羽根を有するドラムを内蔵し、これ
により排気ガスに遠心作用を与えてミストを除去する簡
単な構成のミスト除去装置を提供するにある。This invention was made in view of the above problems, and
The object of the present invention is to provide a mist removing device having a simple structure, which includes a built-in drum having fixed guide vanes, and which applies a centrifugal action to exhaust gas to remove mist.
上記問題点を解決するための手段として、この発明では
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Cご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
して主体内と連通ずる捕集管を配備した構成を採用した
のである。As a means for solving the above problems, the present invention has a cylindrical main body equipped with a drum having a small-diameter discharge cylindrical part at the upper part and a central part C guide vane on the lower gas inflow side, A configuration was adopted in which a collection pipe was placed around the outer periphery of the main body, communicating with the inside of the main body through a window hole provided in the main body.
主体下部のガス流入口から流入する排煙脱硫装置の排気
ガスは、主体内壁とドラムとの隙間を案内羽根により案
内されて渦流となり円運動しながら上昇する。この円運
動をしている間に、排気ガス中に含まれる霧滴などの水
分は遠心作用で主体内部中央部のものも全て主体周壁部
へ移動する。Exhaust gas from the flue gas desulfurization device, which flows in from the gas inlet at the bottom of the main body, is guided by guide vanes through the gap between the inner wall of the main body and the drum, becomes a vortex, and rises while moving in a circular motion. During this circular motion, all moisture such as mist droplets contained in the exhaust gas, including those in the center of the main body, move to the main body peripheral wall due to centrifugal action.
こうして移動した霧滴は遠心力lこよって濃縮されて相
互に凝集、粗大化して旋回運動をしっ\窓孔を通って捕
集管lこ入り、その後系外へ除去される。The mist droplets thus moved are concentrated by the centrifugal force, coagulate and become coarse, undergo a swirling motion, enter the collection tube through the window hole, and are then removed from the system.
一方、霧滴などの水分を除去された排気ガスは有害な成
分を除去されたクリーンな排気として上部吐出円筒から
排出される。On the other hand, the exhaust gas from which moisture such as mist droplets has been removed is discharged from the upper discharge cylinder as clean exhaust gas from which harmful components have been removed.
以下この発明の実施例について添付図を参照して詳細I
こ説明する。The details of the embodiments of this invention will be described below with reference to the accompanying drawings.
I will explain this.
第1図はこの実施例の主要断面図である。1は装置の主
体で、この主体1は上部に小口径の吐出円筒部2を有す
る円筒形から成る。3は主体1の下部中央に設けられた
ドラムで、このドラム3の外周壁には円弧の形をした複
数の案内羽根4を等間隔に配備しである。5は主体1の
外周壁lこ周方向はゾ等間隔lこ設けられた窓孔、6は
窓孔5に連通して主体1の外周壁lこ起立して設けられ
た捕集管、7はこの捕集管6の下部を集合させたドレン
管である。FIG. 1 is a main sectional view of this embodiment. Reference numeral 1 denotes the main body of the apparatus, and the main body 1 has a cylindrical shape with a small-diameter discharge cylindrical portion 2 at the upper part. Reference numeral 3 denotes a drum provided at the center of the lower part of the main body 1, and a plurality of arc-shaped guide vanes 4 are arranged at equal intervals on the outer peripheral wall of the drum 3. Reference numeral 5 indicates window holes provided at equal intervals in the circumferential direction of the outer circumferential wall of the main body 1, reference numeral 6 indicates a collection pipe provided standing upright on the outer circumferential wall of the main body 1 in communication with the window holes 5; is a drain pipe in which the lower part of the collecting pipe 6 is assembled.
第21¥J及び第3図は第1図の線I−I、II−IF
からそれぞれ見た断面図である。21¥J and Figure 3 are lines II-IF of Figure 1.
FIG.
上記の如くなるこの発明は、図示省略の排煙脱硫袋fi
llこよって発生した酸性の霧滴などの水分を含有した
脱硫後の排気ガスAを主体1の下部から流入せしめると
、このガスは主体1内壁とドラム3との隙間を通り、圧
縮されながら案内羽根4Iこガイドされて渦流となり円
運動をする。This invention as described above is based on a flue gas desulfurization bag (not shown).
When the desulfurized exhaust gas A containing moisture such as acidic mist droplets thus generated is allowed to flow in from the bottom of the main body 1, this gas passes through the gap between the inner wall of the main body 1 and the drum 3, and is guided while being compressed. The blades 4I are guided to form a vortex and move in a circular motion.
こうして軸方向の流れとして流入した排気ガスは渦流と
なって円運動をしつ\吐出円筒部2へと排出され、その
間tここの排気ガス中lこ含まれるガスより比重の重い
霧滴等の水分は遠心作用を与えられて主体1の中央部よ
り周壁部へと移動し、このため濃縮されて相互lこ凝集
、粗大化して主体1の内面に沿って旋回運動をしながら
窓孔5を通って捕集管6Iこ入り、ドレン管7に集めら
れて系外へ排出される。In this way, the exhaust gas that has flowed in as an axial flow becomes a vortex flow and is discharged to the discharge cylindrical part 2 while making a circular motion. Moisture is given a centrifugal action and moves from the central part of the main body 1 to the peripheral wall part, and as a result, it is concentrated, coagulates, becomes coarse, and moves around the inner surface of the main body 1, passing through the window hole 5. The water passes through the collection pipe 6I, is collected in the drain pipe 7, and is discharged outside the system.
他方、霧滴等の水分を除去された排気ガスBは、吐出円
筒部2から装置外へ排出される。On the other hand, the exhaust gas B from which moisture such as mist droplets has been removed is discharged from the discharge cylindrical portion 2 to the outside of the apparatus.
なお、前記主体1内に設けた吐出円筒部2は、主体1内
に流入せる排気ガスの流れに若干の抵抗を与えることl
こよって、ドラム30案内羽根4によって付勢される円
運動を助勢せしめるためlこ設けられている。Note that the discharge cylindrical portion 2 provided within the main body 1 is designed to provide some resistance to the flow of exhaust gas flowing into the main body 1.
Therefore, the drum 30 is provided in order to assist the circular motion urged by the guide vanes 4.
以上の如くなるこの発明は、円筒形の主体と、この主体
の下部ガス流入側の中央部に固定案内羽根を設けたドラ
ムを装備し、霧滴等の水分を含有した排気ガスが流入す
ると、この排気ガスははシトラムの径lこ相当する距離
中心部から遠ざかり、周壁部へと移動する。このため、
被分離物の飛距離が短くなり、分離時間が短縮される。This invention as described above is equipped with a cylindrical main body and a drum provided with a fixed guide vane at the center of the lower gas inflow side of the main body, and when exhaust gas containing moisture such as mist drops enters, This exhaust gas moves away from the center by a distance corresponding to the diameter of the citrus and moves toward the peripheral wall. For this reason,
The flying distance of the object to be separated is shortened, and the separation time is shortened.
従って。Therefore.
大容量の排気ガスを短時間Eこ処理することができる。A large volume of exhaust gas can be processed in a short time.
また、案内羽根が等間隔lこ円弧を描いて設けられてい
るため開口断面が縮小されて排気ガスは圧縮され乍ら遠
心力か与えられる。このため排気ガス中の霧滴が一層濃
縮されて衝突が激しくなり、凝集効果が顕著lこ現われ
て微細な霧滴の除去がより一層促進され、捕集分離効率
が格段lこ向上するという極めて優れた実用的効果を有
するものである。In addition, since the guide vanes are arranged in a circular arc at regular intervals, the cross section of the opening is reduced and the exhaust gas is compressed while being given centrifugal force. As a result, the mist droplets in the exhaust gas become more concentrated, the collision becomes more intense, and a remarkable agglomeration effect appears, which further promotes the removal of fine mist droplets and greatly improves the collection and separation efficiency. It has excellent practical effects.
第1図Cま鬼発明の実施例の主要断面図、第2因及び第
3図は第1図の線I−I、If−Ifから見た□断面図
である。FIG. 1 is a main cross-sectional view of the embodiment of the invention, and FIGS. 2 and 3 are cross-sectional views taken along lines II and If-If in FIG.
Claims (2)
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ことを特徴
とするミスト除去装置。(1) A cylindrical main body equipped with a drum with a small diameter discharge cylindrical part on the upper part and a guide vane in the center part on the lower gas inflow side, and a drum provided on the outer periphery of this main body. A mist removal device characterized by having a collection tube communicating with the inside of the main body through a window hole.
る特許請求の範囲第1項に記載のミスト除去装置(2) The mist removing device according to claim 1, wherein the guide vane is fixed to a drum.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5768886A JPS62213819A (en) | 1986-03-13 | 1986-03-13 | Mist removal device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5768886A JPS62213819A (en) | 1986-03-13 | 1986-03-13 | Mist removal device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62213819A true JPS62213819A (en) | 1987-09-19 |
Family
ID=13062882
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5768886A Pending JPS62213819A (en) | 1986-03-13 | 1986-03-13 | Mist removal device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62213819A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2683894A1 (en) * | 1991-11-15 | 1993-05-21 | Sorelec | Installation for cooling and dehydrating hot and humid air |
KR100456911B1 (en) * | 2001-07-06 | 2004-11-10 | 주식회사 시원기업 | Apparatus for Removal with Hazardous Gas for Semi-Dry Scrubber |
JP2007503295A (en) * | 2003-08-26 | 2007-02-22 | ハイドロジェニクス コーポレイション | Energy and / or mass exchanger integrated with fluid separator |
JP2007503296A (en) * | 2003-08-26 | 2007-02-22 | ハイドロジェニクス コーポレイション | Apparatus for separating liquid from process gas stream of an electrochemical cell stack |
JP2008527253A (en) * | 2004-12-30 | 2008-07-24 | ツヴィスター・ベー・ウイ | Throttle valve and method for enlarging droplet size in a flowing fluid stream |
DE102012220186A1 (en) * | 2012-11-06 | 2014-05-08 | Efficient Energy Gmbh | Mist separator and evaporator |
WO2017097185A1 (en) * | 2015-12-08 | 2017-06-15 | 江苏揽山环境科技股份有限公司 | Demister |
TWI665002B (en) * | 2017-09-27 | 2019-07-11 | 大陸商北京中能諾泰節能環保技術有限責任公司 | Dust and mist removal device and absorption tower |
CN116688654A (en) * | 2023-08-04 | 2023-09-05 | 江苏河海新动力有限公司 | Demister and demister |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4216235Y1 (en) * | 1965-01-07 | 1967-09-19 | ||
JPS5514904U (en) * | 1978-07-10 | 1980-01-30 |
-
1986
- 1986-03-13 JP JP5768886A patent/JPS62213819A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4216235Y1 (en) * | 1965-01-07 | 1967-09-19 | ||
JPS5514904U (en) * | 1978-07-10 | 1980-01-30 |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2683894A1 (en) * | 1991-11-15 | 1993-05-21 | Sorelec | Installation for cooling and dehydrating hot and humid air |
KR100456911B1 (en) * | 2001-07-06 | 2004-11-10 | 주식회사 시원기업 | Apparatus for Removal with Hazardous Gas for Semi-Dry Scrubber |
JP2007503295A (en) * | 2003-08-26 | 2007-02-22 | ハイドロジェニクス コーポレイション | Energy and / or mass exchanger integrated with fluid separator |
JP2007503296A (en) * | 2003-08-26 | 2007-02-22 | ハイドロジェニクス コーポレイション | Apparatus for separating liquid from process gas stream of an electrochemical cell stack |
JP2008527253A (en) * | 2004-12-30 | 2008-07-24 | ツヴィスター・ベー・ウイ | Throttle valve and method for enlarging droplet size in a flowing fluid stream |
DE102012220186A1 (en) * | 2012-11-06 | 2014-05-08 | Efficient Energy Gmbh | Mist separator and evaporator |
WO2017097185A1 (en) * | 2015-12-08 | 2017-06-15 | 江苏揽山环境科技股份有限公司 | Demister |
TWI665002B (en) * | 2017-09-27 | 2019-07-11 | 大陸商北京中能諾泰節能環保技術有限責任公司 | Dust and mist removal device and absorption tower |
CN116688654A (en) * | 2023-08-04 | 2023-09-05 | 江苏河海新动力有限公司 | Demister and demister |
CN116688654B (en) * | 2023-08-04 | 2023-10-20 | 江苏河海新动力有限公司 | Demister and demister |
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