JPH04298211A - Scrubber - Google Patents
ScrubberInfo
- Publication number
- JPH04298211A JPH04298211A JP3031812A JP3181291A JPH04298211A JP H04298211 A JPH04298211 A JP H04298211A JP 3031812 A JP3031812 A JP 3031812A JP 3181291 A JP3181291 A JP 3181291A JP H04298211 A JPH04298211 A JP H04298211A
- Authority
- JP
- Japan
- Prior art keywords
- dust removal
- exhaust gas
- cylinder part
- liquid
- dust removing
- 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
- 239000000428 dust Substances 0.000 claims abstract description 60
- 239000007788 liquid Substances 0.000 claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000002347 injection Methods 0.000 claims abstract description 18
- 239000007924 injection Substances 0.000 claims abstract description 18
- 239000003595 mist Substances 0.000 claims abstract description 8
- 230000002093 peripheral effect Effects 0.000 claims abstract description 8
- 239000002699 waste material Substances 0.000 claims abstract description 4
- 239000007921 spray Substances 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 4
- -1 for example Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 239000003929 acidic solution Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は工場等から排出される排
ガスから有害成分や粉塵等を除去するスクラバーに関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a scrubber for removing harmful components, dust, etc. from exhaust gas discharged from factories and the like.
【0002】0002
【従来の技術】一般に、工場等から排出される排ガスに
は有害成分や粉塵を含有することも多いため、これらを
除去するスクラバーが用いられている。2. Description of the Related Art Generally, exhaust gas discharged from factories and the like often contains harmful components and dust, so scrubbers are used to remove these.
【0003】従来、各種のスクラバーが実用化されてい
るが、最も性能の高いスクラバーとしてベンチュリスク
ラバーが知られている。図6は従来におけるベンチュリ
スクラバーの原理構成を示す。同図に示すベンチュリス
クラバー60は絞られたベンチュリ管61に排ガス62
を通過させることにより流速を高め、これに霧状の薬液
(中和液等)63を噴き込むことにより、液体の気体接
触を行って、有害成分や粉塵を除去するものであり、電
気除塵装置に近い除塵効果を得れる。なお、有害成分等
の除去された気体64は排気筒65から外部に排出され
る。Conventionally, various types of scrubbers have been put into practical use, but the Venturi scrubber is known as the scrubber with the highest performance. FIG. 6 shows the basic configuration of a conventional venturi scrubber. The venturi scrubber 60 shown in the same figure has an exhaust gas 62 in a venturi pipe 61 which is constricted.
The electrostatic dust removal device is used to increase the flow rate by passing through the liquid and inject a mist chemical liquid (neutralizing liquid, etc.) 63 into the liquid to bring the liquid into gaseous contact and remove harmful components and dust. You can obtain a dust removal effect close to that of Note that the gas 64 from which harmful components and the like have been removed is discharged to the outside from the exhaust pipe 65.
【0004】0004
【発明が解決しようとする課題】しかし、上述した従来
のベンチュリスクラバー60は比較的高い除塵効率を得
れるものの、ベンチュリ管61の使用が不可欠となるた
め、圧力損失が高くなり、送気系の設備が大型で大掛か
りとなるとともに、エネルギー消費が高くなる難点があ
り、また、除塵効率を高めるにも限界があった。[Problems to be Solved by the Invention] However, although the conventional venturi scrubber 60 described above can obtain relatively high dust removal efficiency, it requires the use of a venturi pipe 61, resulting in high pressure loss and problems with the air supply system. The equipment was large and large-scale, and energy consumption was high, and there was also a limit to how much dust removal efficiency could be achieved.
【0005】本発明はこのような従来の技術に存在する
課題を解決したものであり、設備全体の簡略化とエネル
ギー消費の低減を図り、しかも、高い除塵効率を得れる
スクラバーの提供を目的とする。[0005] The present invention solves the problems that exist in the conventional technology, and aims to provide a scrubber that simplifies the entire equipment, reduces energy consumption, and achieves high dust removal efficiency. do.
【0006】[0006]
【課題を解決するための手段】本発明に係るスクラバー
1は鉛直軸線に対して同軸上に内筒部2と外筒部3を配
することにより、内筒部2と外筒部3間に除塵空間Sp
を設け、除塵空間Spの上端を閉塞し、かつ外筒部3に
おける周面部3fの上端から除塵空間Spの略周方向に
排ガスCを導入可能な排ガス導入口4を臨ませるととも
に、除塵空間Spの下端と内筒部2の下端を相連通し、
かつ外筒部3の下部に所定量の排水(排液)Wtを貯溜
する液溜部8を有する排液部6を設けるとともに、除塵
空間Sp内に、排ガスCの流動方向に除塵用液、例えば
、水Wを霧状に噴出する複数の噴射ノズル7…を配設し
てなることを特徴とする。この場合、噴射ノズル7…は
内筒部2の周面部2f及び(又は)外筒部3の周面部3
fに配設する。[Means for Solving the Problems] The scrubber 1 according to the present invention has an inner cylinder part 2 and an outer cylinder part 3 disposed coaxially with respect to a vertical axis, so that the inner cylinder part 2 and the outer cylinder part 3 are disposed coaxially. Dust removal space Sp
is provided, closes the upper end of the dust removal space Sp, and faces the exhaust gas inlet 4 through which exhaust gas C can be introduced from the upper end of the peripheral surface 3f of the outer cylinder part 3 in a substantially circumferential direction of the dust removal space Sp. and the lower end of the inner cylinder part 2 are connected to each other,
In addition, a liquid drain part 6 having a liquid reservoir part 8 for storing a predetermined amount of waste water (drainage liquid) Wt is provided in the lower part of the outer cylinder part 3, and a dust removal liquid, a dust removal liquid, For example, it is characterized by disposing a plurality of injection nozzles 7 that eject water W in the form of mist. In this case, the injection nozzles 7...
Place it in f.
【0007】[0007]
【作用】本発明に係るスクラバー1によれば、内筒部2
と外筒部3により筒状の除塵空間Spが形成される。し
たがって、除塵空間Spに臨ませた排ガス導入口4から
排ガスCを略周方向に導入すれば、排ガスCは除塵空間
Sp内をスパイラル状に流動して下端に達する。これに
より、排ガスCの流動長は実質的に長くなる。[Operation] According to the scrubber 1 according to the present invention, the inner cylinder part 2
A cylindrical dust removal space Sp is formed by the outer cylinder portion 3 and the outer cylinder portion 3. Therefore, if the exhaust gas C is introduced in a substantially circumferential direction from the exhaust gas inlet 4 facing the dust removal space Sp, the exhaust gas C flows in a spiral shape inside the dust removal space Sp and reaches the lower end. As a result, the flow length of the exhaust gas C becomes substantially longer.
【0008】一方、除塵空間Spの内部では噴射ノズル
7…から排ガスCの流動方向に霧状の水Wを噴出するた
め、霧化された水Wに排ガスCが接触し、排ガスC中か
ら有害成分や粉塵等が除去(洗浄)される。そして、気
体接触を行った後の水Wは排液部6における液溜部8に
収容され、さらに、外部に排出(貯溜)されるとともに
、有害成分等が除去された気体Coは除塵空間Spの下
端から内筒部2の下端に進入し、内筒部2の内部空間を
上昇して外部に排出される。On the other hand, inside the dust removal space Sp, atomized water W is ejected from the injection nozzles 7 in the flow direction of the exhaust gas C, so the exhaust gas C comes into contact with the atomized water W, and harmful substances are removed from the exhaust gas C. Components, dust, etc. are removed (cleaned). After the gas contact, the water W is stored in the liquid storage part 8 in the liquid drainage part 6, and is further discharged (stored) to the outside, and the gas Co from which harmful components have been removed is removed from the dust removal space Sp. The liquid enters the lower end of the inner cylinder part 2 from the lower end of the cylinder, ascends through the internal space of the inner cylinder part 2, and is discharged to the outside.
【0009】この際、除塵空間Spの下端から内筒部2
に至る気体Coの一部は液溜部8における排水Wtの液
面に接触し、有害成分等のさらなる除去が行われる。な
お、噴射ノズル7…を除塵空間Spの内側と外側に配す
れば、除塵空間Sp内に充満する霧のより均一化が図ら
れる。At this time, from the lower end of the dust removal space Sp to the inner cylinder part 2
A part of the gaseous Co that reaches the contact point with the liquid surface of the waste water Wt in the liquid reservoir 8, and further removal of harmful components and the like is performed. Note that if the injection nozzles 7 are arranged inside and outside the dust removal space Sp, the mist filling the dust removal space Sp can be made more uniform.
【0010】0010
【実施例】次に、本発明に係る好適実施例を挙げ、図面
に基づき詳細に説明する。Embodiments Next, preferred embodiments of the present invention will be described in detail with reference to the drawings.
【0011】まず、本発明に係るスクラバー1を含むス
クラバーシステムMの全体構成について、図3〜図5を
参照して説明する。First, the overall configuration of a scrubber system M including the scrubber 1 according to the present invention will be explained with reference to FIGS. 3 to 5.
【0012】1は本発明に係るスクラバーであり、周面
上端には導入ダクト11の一端、即ち、排ガス導入口4
を接続する。また、導入ダクト11の他端は工場等から
排出される排ガスCを吸入する吸入口12となり、導入
ダクト11の中途部には送風機13を設ける。Reference numeral 1 designates a scrubber according to the present invention, and one end of an introduction duct 11, that is, an exhaust gas introduction port 4 is provided at the upper end of the circumferential surface.
Connect. The other end of the introduction duct 11 serves as an inlet 12 for sucking exhaust gas C discharged from factories, etc., and a blower 13 is provided in the middle of the introduction duct 11.
【0013】一方、スクラバー1の上面部中央には有害
成分等の除去された気体Coを排出する排気口5を設け
るとともに、下面部中央には排水パイプ14の一端を接
続する。また、排水パイプ14の他端は浄化槽15の側
面部一側に接続し、排液部6を構成する。この場合、浄
化槽15の水量(水面レベル)は任意に調整でき、これ
により、スクラバー1の底面部に所定量の水Wを貯溜で
きる液溜部8が構成される。また、浄化槽15の側面部
他側には送水パイプ16の一端を接続し、この送水パイ
プ16の他側はポンプ17を介してスクラバー1に接続
する。なお、浄化槽15は排水パイプ14から戻された
水Wを貯溜及び浄化する機能を有し、浄化槽15内部の
中間部には図5に示すフィルター18を設けている。な
お、19はスクラバー1に設けた清掃口である。On the other hand, an exhaust port 5 is provided at the center of the upper surface of the scrubber 1 to discharge gaseous Co from which harmful components have been removed, and one end of a drain pipe 14 is connected to the center of the lower surface. The other end of the drain pipe 14 is connected to one side of the septic tank 15 to form a drain section 6. In this case, the amount of water (water surface level) in the septic tank 15 can be adjusted as desired, thereby forming a liquid reservoir 8 that can store a predetermined amount of water W at the bottom of the scrubber 1. Further, one end of a water pipe 16 is connected to the other side of the septic tank 15, and the other side of the water pipe 16 is connected to the scrubber 1 via a pump 17. Note that the septic tank 15 has a function of storing and purifying the water W returned from the drain pipe 14, and a filter 18 shown in FIG. 5 is provided in the middle part inside the septic tank 15. Note that 19 is a cleaning port provided in the scrubber 1.
【0014】次に、スクラバー1の要部構成について図
1及び図2を参照して説明する。Next, the main structure of the scrubber 1 will be explained with reference to FIGS. 1 and 2.
【0015】スクラバー1は鉛直軸線に対して同軸上に
配した内筒部2と外筒部3を備える。これにより、内筒
部2と外筒部3間には筒状の除塵空間Spが形成される
。除塵空間Spの上端は外筒部3の上端に一体形成した
上面部3uにより閉塞される。また、外筒部3における
周面部3fの上端には前記排ガス導入口4を連通接続す
る。排ガス導入口4は排ガスCを除塵空間Spの略周方
向に対して導入可能に臨ませる。一方、内筒部2の下端
は外筒部3の長さよりも短く形成し、除塵空間Spの下
端と内筒部2における内部空間を相連通させるとともに
、内筒部2の上端は前記排気口5として外部上方に向け
て開口させる。また、外筒部3の下端には下面部3dを
一体形成し、下面部3dの中央に排液部6を構成する前
記排水パイプ14を連通接続する。The scrubber 1 includes an inner cylinder part 2 and an outer cylinder part 3 arranged coaxially with respect to a vertical axis. Thereby, a cylindrical dust removal space Sp is formed between the inner cylinder part 2 and the outer cylinder part 3. The upper end of the dust removal space Sp is closed by an upper surface part 3u integrally formed with the upper end of the outer cylinder part 3. Furthermore, the exhaust gas inlet 4 is connected to the upper end of the peripheral surface portion 3f of the outer cylinder portion 3. The exhaust gas inlet 4 faces the exhaust gas C so that it can be introduced into the dust removal space Sp in a substantially circumferential direction. On the other hand, the lower end of the inner cylinder part 2 is formed shorter than the length of the outer cylinder part 3, so that the lower end of the dust removal space Sp and the internal space of the inner cylinder part 2 are communicated with each other, and the upper end of the inner cylinder part 2 is formed at the exhaust port. 5, it is opened toward the outside and upward. Further, a lower surface portion 3d is integrally formed at the lower end of the outer cylinder portion 3, and the drain pipe 14 constituting the liquid drain portion 6 is connected to the center of the lower surface portion 3d.
【0016】他方、外筒部3における周面部3fの外周
下部には周面に沿った外リングパイプ21を配設すると
ともに、内筒部2における周面部2fの外周下部には周
面に沿った内リングパイプ22をそれぞれ配設し、各外
リングパイプ21と内リングパイプ22には送水パイプ
16を接続する。一方、外リングパイプ21の上面には
複数(例示は四本)の外鉛直パイプ23…をリング方向
に沿って等間隔に設けるとともに、内リングパイプ22
の上面には複数(例示は四本)の内鉛直パイプ24…を
リング方向に沿って等間隔にそれぞれ設け、各内鉛直パ
イプ23…、24…は鉛直方向に立ち上げる。また、内
鉛直パイプ24の長手方向には複数の噴射ノズル7…を
一定間隔置きに設ける。噴射ノズル7…は水Wを霧状に
噴出する機能を有し、噴出方向は除塵空間Spの略周方
向となる排ガスCの流動方向に設定する。さらにまた、
外鉛直パイプ23の長手方向にも内鉛直パイプ24と同
様の機能を有する噴射ノズル7…を一定間隔置きに複数
設ける。この場合、外鉛直パイプ23の噴射ノズル7…
は外筒部3を貫通して内部に臨ませる。また、外鉛直パ
イプ23…と内鉛直パイプ24…は、図2に示すように
除塵空間Spの周方向へそれぞれ交互に配するとともに
、外鉛直パイプ23の噴射ノズル7…と内鉛直パイプ2
4の噴射ノズル7…は上下方向へそれぞれ交互に配し、
各噴射ノズル7…からの霧が除塵空間Sp内に均一に充
満するように考慮する。なお、内リングパイプ22は排
ガスCの流動を阻害しないように内筒部2の内周面に設
け、噴射ノズル7…は内筒部2を貫通させて除塵空間S
pに臨ませてもよい。On the other hand, an outer ring pipe 21 is disposed along the outer periphery of the circumferential surface portion 3f of the outer cylindrical portion 3, and an outer ring pipe 21 is disposed along the outer periphery of the circumferential surface portion 2f of the inner cylindrical portion 2. A water supply pipe 16 is connected to each outer ring pipe 21 and inner ring pipe 22. On the other hand, a plurality of (four in the example) outer vertical pipes 23 are provided on the upper surface of the outer ring pipe 21 at equal intervals along the ring direction, and the inner ring pipe 22
A plurality (four in the example) of inner vertical pipes 24 are provided at equal intervals along the ring direction on the upper surface of the ring, and each of the inner vertical pipes 23..., 24 stands up in the vertical direction. Further, a plurality of injection nozzles 7 are provided at regular intervals in the longitudinal direction of the inner vertical pipe 24. The injection nozzles 7 have a function of ejecting water W in the form of mist, and the ejection direction is set in the flow direction of the exhaust gas C, which is approximately the circumferential direction of the dust removal space Sp. Furthermore,
Also in the longitudinal direction of the outer vertical pipe 23, a plurality of injection nozzles 7 having the same function as the inner vertical pipe 24 are provided at regular intervals. In this case, the injection nozzle 7 of the outer vertical pipe 23...
penetrates the outer cylindrical portion 3 and faces inside. Further, the outer vertical pipes 23... and the inner vertical pipes 24... are arranged alternately in the circumferential direction of the dust removal space Sp as shown in FIG.
No. 4 injection nozzles 7 are arranged alternately in the vertical direction,
Consideration is given so that the mist from each injection nozzle 7 uniformly fills the dust removal space Sp. The inner ring pipe 22 is provided on the inner circumferential surface of the inner cylinder part 2 so as not to obstruct the flow of the exhaust gas C, and the injection nozzles 7 are inserted into the dust removal space S by penetrating the inner cylinder part 2.
You may also have them face p.
【0017】次に、スクラバー1を含むスクラバーシス
テムM全体の動作及び機能について説明する。Next, the operation and function of the entire scrubber system M including the scrubber 1 will be explained.
【0018】まず、送風機13の作動により工場等から
排出された排ガスCは吸入口12から吸入される。そし
て、排ガスCは導入ダクト11を通って排ガス導入口4
から除塵空間Spの上端に導入される。排ガスCは筒状
の除塵空間Spの略周方向に導入されるため、図1及び
図2に矢印Hで示すように除塵空間Sp内をスパイラル
状に流動し、下端に達する。これにより、排ガスCの流
動長は実質的に長くなる。一方、各噴射ノズル7…から
は排ガスCの流動方向に対して霧状の水Wを噴出するた
め、除塵空間Sp内では霧化された水Wに排ガスCが接
触し、排ガスC中の有害成分や粉塵等が除去(洗浄)さ
れる。なお、この場合、通常は中和液等の薬液が用いら
れるが、本スクラバー1を比較的低濃度の排ガスに用い
れば、水Wでも十分な除塵効果を得れる。そして、有害
成分等が除去された気体Coは除塵空間Spの下端から
内筒部2の下端からその内部空間に進入し、内筒部2の
内部空間を上昇して排気口5から外部に排出される。First, exhaust gas C discharged from a factory or the like by the operation of the blower 13 is sucked in through the suction port 12 . Then, the exhaust gas C passes through the introduction duct 11 and the exhaust gas inlet 4
is introduced into the upper end of the dust removal space Sp. Since the exhaust gas C is introduced in the substantially circumferential direction of the cylindrical dust removal space Sp, it flows in the dust removal space Sp in a spiral shape as shown by the arrow H in FIGS. 1 and 2, and reaches the lower end. As a result, the flow length of the exhaust gas C becomes substantially longer. On the other hand, since atomized water W is ejected from each injection nozzle 7 in the flow direction of the exhaust gas C, the exhaust gas C comes into contact with the atomized water W in the dust removal space Sp. Components, dust, etc. are removed (cleaned). In this case, a chemical liquid such as a neutralizing liquid is usually used, but if the present scrubber 1 is used for exhaust gas with a relatively low concentration, a sufficient dust removal effect can be obtained even with water W. Then, the gas Co from which harmful components have been removed enters the internal space from the lower end of the dust removal space Sp and the lower end of the inner cylinder part 2, rises in the inner space of the inner cylinder part 2, and is discharged to the outside from the exhaust port 5. be done.
【0019】一方、気体接触を行った後の有害成分等を
含む排水Wtは、排液部6における液溜部8に収容され
、さらに排水パイプ14を通って浄化槽15に流入し、
浄化槽15において簡易浄化される。即ち、排水Wt中
の比較的大きい固形物は浄化槽15内に沈殿し、小さい
固形物はフィルター18によって除去される。On the other hand, the waste water Wt containing harmful components etc. after the gas contact is stored in the liquid reservoir part 8 in the drain part 6, and further flows into the septic tank 15 through the drain pipe 14.
It is simply purified in the septic tank 15. That is, relatively large solids in the waste water Wt settle in the septic tank 15, and small solids are removed by the filter 18.
【0020】なお、外筒部3の下方には液溜部8が存在
するため、気体Coは除塵空間Spの下端から内筒部2
に至る際に、さらに液溜部8に収容された排水Wtの水
面に接触して有害成分等が除去される。この液溜部8の
水量は調節が可能であり、水量調整により水面を上昇さ
せれば、通気路が狭くなり、下降させれば、通気路は広
くなるため、除塵効率、排ガスCの流動速度(圧力損失
)等を細かく調節できる。また、浄化処理された浄化槽
15中の排水Wtはポンプ17によって、送水パイプ1
6を介して前記外リングパイプ21及び内リングパイプ
22に再び送られ、噴射ノズル7…から噴出される。[0020] Since the liquid reservoir 8 exists below the outer cylinder part 3, the gas Co flows from the lower end of the dust removal space Sp to the inner cylinder part 2.
At the time of reaching this point, the water further comes into contact with the water surface of the waste water Wt accommodated in the liquid reservoir 8, and harmful components and the like are removed. The amount of water in this liquid reservoir 8 can be adjusted, and if the water level is raised by adjusting the water amount, the ventilation path will be narrowed, and if it is lowered, the ventilation path will be widened. (pressure loss) etc. can be finely adjusted. Further, the purified waste water Wt in the septic tank 15 is transferred to the water pipe 1 by the pump 17.
6 to the outer ring pipe 21 and inner ring pipe 22, and is ejected from the injection nozzles 7.
【0021】このようなスクラバー1は圧力損失が極め
て小さくなり、しかも、排ガスCの流動経路はスパイラ
ル状になるため、実質的な流動長を長くでき、除塵効率
が高められる。[0021] In such a scrubber 1, the pressure loss is extremely small, and since the flow path of the exhaust gas C is spiral-shaped, the substantial flow length can be increased, and the dust removal efficiency can be increased.
【0022】以上、実施例について詳細に説明したが、
本発明はこのような実施例に限定されるものではない。
例えば、水の代わりに酸性溶液、アルカリ性溶液等の薬
液を用いても勿論よい。また、噴射ノズルは内筒部側又
は外筒部側のいずれか一方であってもよい。その他、細
部の構成、形状、数量等において、本発明の要旨を逸脱
しない範囲で任意に変更できる。The embodiments have been described in detail above, but
The invention is not limited to such embodiments. For example, it is of course possible to use a chemical solution such as an acidic solution or an alkaline solution instead of water. Further, the injection nozzle may be located on either the inner cylinder side or the outer cylinder side. In addition, the detailed configuration, shape, quantity, etc. may be arbitrarily changed without departing from the gist of the present invention.
【0023】[0023]
【発明の効果】このように、本考案に係るスクラバーは
内筒部と外筒部間に除塵空間を設け、除塵空間の上端を
閉塞し、かつ外筒部における周面部の上端から除塵空間
の略周方向に排ガスを導入可能な排ガス導入口を臨ませ
るとともに、除塵空間の下端と内筒部の下端を相連通し
、かつ外筒部の下部に所定量の排液を貯溜する液溜部を
有する排液部を設けるとともに、除塵空間内に、排ガス
の流動方向に除塵用液を霧状に噴出する複数の噴射ノズ
ルを配設してなるため、従来のようなベンチュリ管が不
要となり、圧力損失の著しい減少に伴う設備全体の簡略
化とエネルギー消費の低下を図れ、しかも、高い除塵効
率を得れるという顕著な効果を奏する。As described above, the scrubber according to the present invention provides a dust removal space between the inner cylinder part and the outer cylinder part, closes the upper end of the dust removal space, and opens the dust removal space from the upper end of the peripheral surface of the outer cylinder part. An exhaust gas inlet that can introduce exhaust gas in a substantially circumferential direction faces the exhaust gas inlet, the lower end of the dust removal space and the lower end of the inner cylinder part are connected to each other, and a liquid reservoir part for storing a predetermined amount of waste liquid is provided at the lower part of the outer cylinder part. In addition to providing a drainage section with a liquid discharger, multiple injection nozzles are installed in the dust removal space to spray dust removal liquid in the form of a mist in the flow direction of the exhaust gas, eliminating the need for a conventional Venturi tube and reducing pressure. This has the remarkable effect of simplifying the entire equipment and lowering energy consumption due to a significant reduction in losses, as well as achieving high dust removal efficiency.
【図1】本発明に係るスクラバーの縦断面図、FIG. 1 is a vertical cross-sectional view of a scrubber according to the present invention;
【図2】
同スクラバーの横断面図、[Figure 2]
Cross-sectional view of the same scrubber,
【図3】同スクラバーを含むスクラバーシステムの正面
図、[Fig. 3] Front view of a scrubber system including the same scrubber,
【図4】同スクラバーシステムの平面図、[Fig. 4] Plan view of the scrubber system,
【図5】同ス
クラバーシステムにおける水槽の断面側面図、[Fig. 5] Cross-sectional side view of the water tank in the same scrubber system,
【図6】従来の技術に係るベンチュリスクラバーの原理
構成図、[Fig. 6] Principle configuration diagram of a venturi scrubber according to conventional technology,
1 スクラバー 2 内筒部 2f 周面部 3 外筒部 3f 周面部 4 排ガス導入口 6 排液部 7 噴射ノズル 8 液溜部 Sp 除塵空間 C 排ガス W 水 Wt 排水 1 Scrubber 2 Inner cylinder part 2f Peripheral part 3 Outer cylinder part 3f Peripheral part 4 Exhaust gas inlet 6 Drainage part 7 Injection nozzle 8 Liquid reservoir Sp Dust removal space C Exhaust gas W Water Wt drainage
Claims (4)
筒部を配することにより、内筒部と外筒部間に除塵空間
を設け、除塵空間の上端を閉塞し、かつ外筒部における
周面部の上端から除塵空間の略周方向に排ガスを導入可
能な排ガス導入口を臨ませるとともに、除塵空間の下端
と内筒部の下端を相連通し、かつ外筒部の下部に、所定
量の排液を貯溜可能な液溜部を有する排液部を設けると
ともに、除塵空間内に、排ガスの流動方向へ除塵用液を
霧状に噴出する複数の噴射ノズルを配設してなることを
特徴とするスクラバー。Claim 1: By arranging the inner cylinder part and the outer cylinder part coaxially with respect to the vertical axis, a dust removal space is provided between the inner cylinder part and the outer cylinder part, the upper end of the dust removal space is closed, and the outer cylinder part is arranged coaxially with respect to the vertical axis. An exhaust gas inlet that can introduce exhaust gas in the general circumferential direction of the dust removal space faces from the upper end of the peripheral surface of the cylinder part, and the lower end of the dust removal space and the lower end of the inner cylinder part are connected to each other, and at the bottom of the outer cylinder part, A liquid drainage part having a liquid reservoir capable of storing a predetermined amount of waste liquid is provided, and a plurality of spray nozzles are arranged in the dust removal space to spray dust removal liquid in the form of mist in the flow direction of the exhaust gas. A scrubber characterized by:
請求項1記載のスクラバー。2. The scrubber according to claim 1, wherein water is used as the dust removal liquid.
は)外筒部の周面部に配設することを特徴とする請求項
1記載のスクラバー。3. The scrubber according to claim 1, wherein the injection nozzle is disposed on the circumferential surface of the inner cylindrical portion and/or on the circumferential surface of the outer cylindrical portion.
に構成することを特徴とする請求項1記載のスクラバー
。4. The scrubber according to claim 1, wherein the amount of waste liquid stored in the liquid reservoir is configured to be adjustable.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3031812A JPH04298211A (en) | 1991-01-30 | 1991-01-30 | Scrubber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3031812A JPH04298211A (en) | 1991-01-30 | 1991-01-30 | Scrubber |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04298211A true JPH04298211A (en) | 1992-10-22 |
Family
ID=12341505
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3031812A Pending JPH04298211A (en) | 1991-01-30 | 1991-01-30 | Scrubber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04298211A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100395376B1 (en) * | 2000-10-24 | 2003-08-21 | 엠에이티 주식회사 | Gas Scrubber with auto disassembling device |
-
1991
- 1991-01-30 JP JP3031812A patent/JPH04298211A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100395376B1 (en) * | 2000-10-24 | 2003-08-21 | 엠에이티 주식회사 | Gas Scrubber with auto disassembling device |
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