JPH0639774Y2 - Exhaust gas purification device - Google Patents

Exhaust gas purification device

Info

Publication number
JPH0639774Y2
JPH0639774Y2 JP4476793U JP4476793U JPH0639774Y2 JP H0639774 Y2 JPH0639774 Y2 JP H0639774Y2 JP 4476793 U JP4476793 U JP 4476793U JP 4476793 U JP4476793 U JP 4476793U JP H0639774 Y2 JPH0639774 Y2 JP H0639774Y2
Authority
JP
Japan
Prior art keywords
exhaust gas
gas
liquid
cleaning liquid
cleaning
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
JP4476793U
Other languages
Japanese (ja)
Other versions
JPH0624724U (en
Inventor
隆志 富松
繁 濱名
直恭 山本
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.)
Seikow Chemical Engr and Machinery Ltd
Original Assignee
Seikow Chemical Engr and Machinery Ltd
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 Seikow Chemical Engr and Machinery Ltd filed Critical Seikow Chemical Engr and Machinery Ltd
Priority to JP4476793U priority Critical patent/JPH0639774Y2/en
Publication of JPH0624724U publication Critical patent/JPH0624724U/en
Application granted granted Critical
Publication of JPH0639774Y2 publication Critical patent/JPH0639774Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】この考案は微細なミストやヒュー
ムを有害成分として含有する排ガスを浄化する排ガス浄
化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas purifying apparatus for purifying exhaust gas containing fine mist and fumes as harmful components.

【0002】[0002]

【従来の技術】最近の金属や半導体の表面処理工程で
は、塩酸、硫酸、硝酸などの酸洗浄液を使用して高温浴
下で表面処理することが多く、この排ガス系統では反応
生成ガスの他に前記酸性ガスの蒸気が絶えず排ガス中に
同伴して排出されているのが現状である。
2. Description of the Related Art In recent surface treatment processes for metals and semiconductors, acid cleaning liquids such as hydrochloric acid, sulfuric acid and nitric acid are often used for surface treatment in a high temperature bath. The present situation is that the vapor of the acidic gas is constantly discharged along with the exhaust gas.

【0003】これらの排ガスは、従来より、比較的簡易
な充填塔や多孔塔などの湿式洗浄塔で大部分は処理され
ている。
Most of these exhaust gases have conventionally been treated in a relatively simple wet tower such as a packed tower or a porous tower.

【0004】[0004]

【考案が解決しようとする課題】ところが上記する湿式
洗浄塔による処理では、処理塔内の湿分と酸性ガスとが
会合して生成するエアロゾル状の微細なミストは排出側
のミストセパレータでも捕集することができず、煙突で
白煙霧化して視界を妨げたり、周辺地域にたれこめたり
して公害上から問題がある。
However, in the treatment by the wet cleaning tower described above, fine aerosol-like mist generated by the association of the moisture and the acid gas in the treatment tower is collected by the mist separator on the discharge side. It is not possible to do so, and there is a problem in terms of pollution, such as white smoke atomizing in the chimney, obstructing the field of view, and hanging up in the surrounding area.

【0005】この白煙霧化したエアロゾルを除去するた
めには、湿式洗浄装置の後段に高性能のフィルターや電
気集塵機などの高性能な除塵機能を持つ装置を付加的に
設置するほか解決手段はなく、これらは新たに大きな設
置スペースを必要とし、処理設備のイニシャルコストお
よびランニングコストなどの経費が高くつき、既設の排
気設備の改良は勿論のこと、新規排気設備の公害防止上
の対策としては容易に実施し得ないものである。
In order to remove the aerosol that has been atomized into white smoke, there is no means for solving the problem except to additionally install a device having a high-performance dust removing function such as a high-performance filter or an electrostatic precipitator after the wet cleaning device. However, these require a new large installation space, and the costs such as the initial cost and running cost of the processing equipment are high, and it is easy to improve the existing exhaust equipment and to prevent pollution of the new exhaust equipment. Cannot be carried out.

【0006】また、微細な粉塵を含有するガスを処理す
る湿式集塵機としては送風機の回転翼に直接、液をスプ
レーするものも従来からあるが、前記の白煙霧化する排
ガスに対しての浄化効果は不充分であり、浄化効果が充
分な程度にまで排ガス処理をしようとすれば他の湿式洗
浄法ないしは電気集塵機の付加が必要であった。
Further, as a wet dust collector for treating a gas containing fine dust, there has been a conventional one in which a liquid is sprayed directly on a rotary blade of a blower. Is insufficient, and in order to treat the exhaust gas to the extent that the purification effect is sufficient, another wet cleaning method or the addition of an electrostatic precipitator was required.

【0007】この考案は上述の点に鑑み考案されたもの
であって、除去困難なエアロゾル状の白煙霧化を形成す
る酸性ガスを含有する排ガスの処理手段について鋭意研
究した結果、従来の湿式洗浄法のみでは不可能とされて
いた前記排ガスを高能率に処理可能とした排ガス浄化装
置を提供することを目的とする。
The present invention has been made in view of the above points, and as a result of earnest research on means for treating exhaust gas containing acid gas which forms aerosol-like white smoke atomization that is difficult to remove, the conventional wet cleaning It is an object of the present invention to provide an exhaust gas purifying apparatus capable of treating the exhaust gas with high efficiency, which has been impossible by the method alone.

【0008】[0008]

【課題を解決するための手段】上記の目的を達成するた
めのこの考案の要旨とするところは、排ガスの吸込口と
吐出口を有する渦巻き筒体内に遠心回転羽根車を具備し
たものにおいて、吸込口前段に洗浄液ノズルを配設する
とともに、排ガスと洗浄液ノズルより噴霧された液を強
制的に通過接触させる多数の小孔を全面に有する多孔円
板を配設したことを特徴とする排ガス浄化装置にある。
Means for Solving the Problems The gist of the present invention for achieving the above-mentioned object is to provide a centrifugal rotary impeller provided in a spiral cylinder having a suction port and a discharge port for exhaust gas. An exhaust gas purifying apparatus characterized in that a cleaning liquid nozzle is arranged in front of the mouth, and a porous disc having a large number of small holes for forcibly passing and contacting the exhaust gas and the liquid sprayed from the cleaning liquid nozzle is arranged. It is in.

【0009】[0009]

【作用】排ガスを吸込口の前段で洗浄液ノズルより噴霧
された液と接触させ、この気液混流物を多孔円板に全面
散布させて強制的に通過させ、吸込口から渦巻き筒体内
に装備された遠心回転羽根車に吸引させて混合撹拌し、
排ガス中の有害成分を吸収および凝集分離除去し、吐出
口より清浄ガスを排出させる。
[Operation] Exhaust gas is brought into contact with the liquid sprayed from the cleaning liquid nozzle before the suction port, and this gas-liquid mixture is sprayed over the perforated disk to forcefully pass it through. The centrifugal rotary impeller is sucked and mixed and stirred,
Absorbs and aggregates and removes harmful components in exhaust gas, and discharges clean gas from the discharge port.

【0010】[0010]

【実施例】以下、この考案の実施例を図面に基づいて説
明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An embodiment of the present invention will be described below with reference to the drawings.

【0011】図1はこの考案の排ガス浄化装置の構成図
である。
FIG. 1 is a block diagram of the exhaust gas purifying apparatus of the present invention.

【0012】この考案の排ガス浄化装置は、排ガス吸込
口1、排ガス吐出口2を有する渦巻き筒体3、および前
記渦巻き筒体3内に回転可能に配設された遠心回転羽根
車4、前記排ガス吸込口1の前段に配設された洗浄液ノ
ズル5、全面に多数の小孔6を有する多孔円板7よりな
る。
The exhaust gas purifying apparatus of the present invention comprises a spiral cylinder 3 having an exhaust gas inlet 1, an exhaust gas discharge port 2, a centrifugal rotary impeller 4 rotatably disposed in the spiral cylinder 3, the exhaust gas. The cleaning liquid nozzle 5 is arranged in front of the suction port 1, and the perforated disk 7 has a large number of small holes 6 on the entire surface.

【0013】洗浄液ノズル5は多孔円板7に対向して該
円板7の全面に液が噴霧されるように少なくとも1つ以
上設けられる。この洗浄液ノズル5からの洗浄液の噴霧
方法としては、微細な洗浄液を作りだす手段であればど
のような手段でも差支えなく、洗浄液のみを噴霧する一
流体ノズル、圧縮空気と洗浄液を混合して出す二流体ノ
ズル、超音波微粒子ノズルなどを用いることができる。
At least one cleaning liquid nozzle 5 is provided so as to face the porous disc 7 so that the liquid is sprayed onto the entire surface of the disc 7. As a method of spraying the cleaning liquid from the cleaning liquid nozzle 5, any means can be used as long as it is a means for producing a fine cleaning liquid, and a one-fluid nozzle for spraying only the cleaning liquid and a two-fluid for mixing compressed air and the cleaning liquid A nozzle, an ultrasonic fine particle nozzle, or the like can be used.

【0014】多孔円板7は吸込口1内に設けられるが、
ガスの通過風速が最も速くなる最小絞り部分に設けるこ
とが気液接触効果を高めるうえから望ましい。小孔6の
形状は丸孔、楕円孔、矩形孔、長矩形孔などを用いるこ
とができるが、目詰まり防止、低圧力損失の面からする
と丸孔のものが好ましく、流路抵抗を少なくするため、
テーパあるいはベルマウス状の孔を用いることもでき
る。そして、小孔6の配置は円板7全面に気液が均等に
分散するように均等な間隔に配置されることが望まし
い。
The porous disc 7 is provided in the suction port 1,
It is desirable to provide it in the smallest throttle portion where the gas passing wind speed becomes the highest in order to enhance the gas-liquid contact effect. The shape of the small hole 6 may be a round hole, an elliptical hole, a rectangular hole, an oblong hole or the like, but from the viewpoint of preventing clogging and low pressure loss, a round hole is preferable and the flow path resistance is reduced. For,
Taper or bellmouth shaped holes can also be used. The small holes 6 are preferably arranged at even intervals so that the gas and liquid are evenly dispersed on the entire surface of the disc 7.

【0015】例えば、小孔を通過するガス流速は30m
/sec 以上が好ましい。小孔6の最小寸法は0.1〜3
0mm、開口比5〜50%のものが使用可能であるが、静
圧損失や気液接触効果を考慮した場合、0.5〜20m
m、開口比10〜40%のものが好ましい。
For example, the gas flow rate through the small holes is 30 m.
/ Sec or more is preferable. The minimum size of the small hole 6 is 0.1-3
It is possible to use 0 mm and an aperture ratio of 5 to 50%, but considering static pressure loss and gas-liquid contact effect, 0.5 to 20 m
Those having m and an aperture ratio of 10 to 40% are preferable.

【0016】また、多孔円板2の構成材としてはプラス
チック、金属、セラミック、ガラス等の耐蝕材料が利用
できる。また、板材を加工したものの他にプラスチッ
ク、金属、セラミック、ガラス等の小粒径物質を焼結積
層した多孔質材料や連続気泡の空隙を有する多孔質材料
を用いることができる。流路抵抗が少なく、気液接触材
料としては、プラスチックを真球状のパール重合粒体を
積層したものを用いれば好適である。さらに、他の板材
としては前記プラスチック、金属、セラミック、ガラス
等の繊維を網状に平面状に構成したものや多層に重ねた
り、立体的に編み、比較的均等な空隙をもつ材料を用い
ることができる。
Further, as a constituent material of the porous disc 2, a corrosion resistant material such as plastic, metal, ceramic, glass or the like can be used. In addition to the processed plate material, a porous material obtained by sintering and laminating a small particle size material such as plastic, metal, ceramic, or glass, or a porous material having open cell voids can be used. As a gas-liquid contact material having a small flow path resistance, it is preferable to use a material obtained by laminating plastic with spherical spherical pearl polymer particles. Further, as the other plate material, it is possible to use a material in which fibers of the above-mentioned plastic, metal, ceramics, glass, etc. are formed in a net-like plane shape, or to be laminated in multiple layers or three-dimensionally knitted and have relatively uniform voids. it can.

【0017】遠心回転羽根車4は具体的には図示しない
が、主板、副板および羽根から構成され、羽根車中心か
らガスを吸い込み、遠心方向に吐き出す周知構成のもの
で、翼形状としては放射状に伸びる径向き羽根、後向き
羽根、前向き羽根等を用いることができるが、特にガス
中に付着性の粉体や不純物が同伴する場合には羽根付着
時のアンバランスを防止するために径向き羽根が望まし
い。
Although not specifically shown, the centrifugal rotary impeller 4 is composed of a main plate, a sub plate, and a blade, has a well-known structure that sucks gas from the center of the impeller and discharges it in the centrifugal direction, and its blade shape is radial. It is possible to use radial blades, rearward blades, frontward blades, etc. that extend in the direction of the blade, but in order to prevent imbalance when the blades adhere, especially when adhering powder or impurities are entrained in the gas. Is desirable.

【0018】渦巻き筒体3は水平あるいは垂直いずれの
方向でもかまわないが、気液の分離を容易にするため
に、渦巻き筒体3を垂直配置にして液流が停滞しないよ
うに吐出口2を横向きまたは下向きにするのが望まし
い。
The spiral cylinder 3 may be either horizontal or vertical, but in order to facilitate the separation of gas and liquid, the spiral cylinder 3 is arranged vertically so that the discharge port 2 is provided so that the liquid flow does not become stagnant. It is desirable to have it face down or sideways.

【0019】上記構成において、酸性ガスを含有する排
ガスは、渦巻き筒体3の吸込口1前段において洗浄液ノ
ズル5より噴霧された液と並流して気液接触を行いなが
ら多孔円板7に対して全面散布され、該円板7の小孔6
を強制的に通過することにより混合して微細な液滴に再
分散されてガス吸収と白煙の凝集が行われ、引き続いて
この気液混流物は吸込口1から渦巻き筒体3に吸い込ま
れる。渦巻き筒体3内では遠心回転羽根車4が高速で回
転しているので、前記の気液の混流物はきわめて激しい
遠心回転力を与えられながら円周方向に流れて混合撹拌
が行われるため、有害ガス成分の吸収および白煙霧体の
凝集成長が行われ、前記有害成分を収集した液成分は渦
巻き室内でガス成分との質量差により分離されて吐出口
2からは清浄なガス成分だけが排出され、液成分は液流
となり排出される
In the above-mentioned structure, the exhaust gas containing the acidic gas flows in parallel with the liquid sprayed from the cleaning liquid nozzle 5 in the preceding stage of the suction port 1 of the spiral tube 3 while making gas-liquid contact with the porous disk 7. The small holes 6 of the circular plate 7 are sprayed over the entire surface.
Are forcibly passed through to be mixed and re-dispersed into fine droplets to absorb gas and agglomerate white smoke, and subsequently this gas-liquid mixture is sucked from the suction port 1 into the spiral tube body 3. . Since the centrifugal rotary impeller 4 rotates at a high speed in the spiral tube body 3, the gas-liquid mixed flow flows in the circumferential direction while being subjected to an extremely vigorous centrifugal rotation force to perform mixing and stirring. The harmful gas component is absorbed and the white smoke body is coagulated and grown, and the liquid component collecting the harmful component is separated by the mass difference from the gas component in the swirl chamber, and only the clean gas component is discharged from the discharge port 2. Liquid component is discharged as a liquid flow

【0020】[0020]

【考案の効果】上記構成からなるこの考案によれば、次
のような効果を奏する。
According to the present invention having the above structure, the following effects can be obtained.

【0021】(1) 従来の湿式洗浄装置では完全に除
去不可能であった白煙霧化する酸性成分を含む排ガスを
高い除去効率で除き、煙突で白煙を目立たなくすること
ができるので、高価な電気集塵機付加する必要がなく公
害防止対策費も少なくて済みきわめて経済効果も大き
い。
(1) White smoke can be made inconspicuous by a chimney by removing with high removal efficiency exhaust gas containing an acidic component that atomizes white smoke, which cannot be completely removed by a conventional wet cleaning apparatus, and is therefore expensive. There is no need to add an electric dust collector, and the cost of pollution prevention measures is low, and the economic effect is extremely large.

【0022】また、遠心回転羽根車直前の多孔円板はマ
ルチベンチュリーに似た気液の激しい混流による気液の
均等な分散を行う効果を有しているで、装置の大小に関
わらず、安定した性能を確保することできる。また、遠
心回転羽根車は液によって常時、洗浄されているので、
ガス中に粘着性の粉塵があってもこれを洗い流し、粉体
付着によるアンバランスも防止でき、保守管理も容易で
ある。
Further, the porous disk immediately before the centrifugal rotary impeller has an effect similar to that of a multi-venturi to evenly disperse gas and liquid by violent mixing of gas and liquid, so that it is stable regardless of the size of the apparatus. It is possible to secure the required performance. Also, since the centrifugal rotary impeller is always washed with liquid,
Even if there is sticky dust in the gas, it can be washed away, imbalance due to powder adhesion can be prevented, and maintenance management is easy.

【0023】さらに、この考案の装置は単独で用いる以
外に入口濃度が異常に高い場合には前処理用として湿式
洗浄塔を設けることができ、後続には筒体内で分離しき
れない液滴をとるエリミネータを設置することにより、
より排ガス浄化効果を高めることができる。
Further, the apparatus of the present invention can be provided with a wet washing tower for pretreatment when the concentration of the inlet is abnormally high in addition to being used alone, and the liquid droplets which cannot be separated in the cylinder are subsequently provided. By installing the Tori Eliminator,
The exhaust gas purification effect can be further enhanced.

【0024】(2) 従来の充填塔その他の湿式洗浄装
置に比較して排ガス中の有害ガス成分を高能率に除去で
きるだけではなく、同伴するサブミクロンサイズのエア
ロゾル状の白煙霧体も有効に除去できる。また、硝酸、
塩酸、硫酸などの蒸気発生ガスの他、微粒子のエアロゾ
ルを生じ、通常、除去困難とされている過塩素酸の煮沸
時の発生ガスに対しても有効に働き、各種エアロゾルに
対しても清浄化効果を期待できる。さらに、排ガスに同
伴する粉塵に対しても除去効果は高く、従来の湿式洗浄
機ではほとんど素通りしていたサブミクロンサイズのシ
リカ、塩化アンモニウム、硝酸アンモニウムなどの固体
エアロゾルに対しても除去効果を有している。
(2) Not only the harmful gas components in the exhaust gas can be removed with high efficiency as compared with the conventional packed tower and other wet cleaning devices, but also the entrained submicron-sized aerosol-like white smoke bodies are effectively removed. it can. Also nitric acid,
In addition to vapor-generated gases such as hydrochloric acid and sulfuric acid, it also produces fine particle aerosols, which works effectively against gas generated during boiling of perchloric acid, which is usually difficult to remove, and also cleans various aerosols. You can expect an effect. Furthermore, it has a high effect of removing dust that accompanies exhaust gas, and also has an effect of removing solid aerosols of submicron-sized silica, ammonium chloride, ammonium nitrate, etc. that were almost passed through by conventional wet cleaning machines. ing.

【0025】(3) 半導体製造、金属酸洗、メッキな
どの工程のように各種有害ガスのほかに液体エアロゾル
や固定エアロゾルが同伴するケースが多い場合の排気洗
浄装置として従来の湿式洗浄機に比べ、浄化機能面で優
れており、高性能の電気集塵機の付加が不用であるの
で、経済的メリットも大きい。
(3) Compared with the conventional wet cleaning machine as an exhaust cleaning device when there are many cases in which liquid aerosol or fixed aerosol is entrained in addition to various harmful gases such as semiconductor manufacturing, metal pickling and plating processes. It is excellent in terms of purification function and does not require the addition of a high-performance electrostatic precipitator, so it has great economic merit.

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

【図1】 この考案の排ガス浄化装置の構成図である。FIG. 1 is a configuration diagram of an exhaust gas purifying apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1…排ガス吸込口 2…排ガス吐出口 3…渦巻き筒体 4…回転羽根車 5…洗浄液ノズル 6…小孔 7…多孔円板 DESCRIPTION OF SYMBOLS 1 ... Exhaust gas inlet 2 ... Exhaust gas outlet 3 ... Spiral cylinder 4 ... Rotating impeller 5 ... Cleaning liquid nozzle 6 ... Small hole 7 ... Perforated disk

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 排ガスの吸込口と吐出口を有する渦巻き
筒体内に遠心回転羽根車を具備したものにおいて、吸込
口前段に洗浄液ノズルを配設するとともに、排ガスと洗
浄液ノズルより噴霧された液を強制的に通過接触させる
多数の小孔を全面に有する多孔円板を配設したことを特
徴とする排ガス浄化装置。
1. A centrifugal impeller provided in a spiral cylinder having a suction port and a discharge port for exhaust gas, wherein a cleaning liquid nozzle is arranged in front of the suction port, and the exhaust gas and the liquid sprayed from the cleaning liquid nozzle are provided. An exhaust gas purifying apparatus, characterized in that a perforated disk having a large number of small holes forcibly passing through and contacting is disposed.
JP4476793U 1993-08-17 1993-08-17 Exhaust gas purification device Expired - Lifetime JPH0639774Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4476793U JPH0639774Y2 (en) 1993-08-17 1993-08-17 Exhaust gas purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4476793U JPH0639774Y2 (en) 1993-08-17 1993-08-17 Exhaust gas purification device

Publications (2)

Publication Number Publication Date
JPH0624724U JPH0624724U (en) 1994-04-05
JPH0639774Y2 true JPH0639774Y2 (en) 1994-10-19

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JP4476793U Expired - Lifetime JPH0639774Y2 (en) 1993-08-17 1993-08-17 Exhaust gas purification device

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Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4782722B2 (en) * 2007-04-18 2011-09-28 フルタ電機株式会社 High temperature steam or contaminated steam processor
JP5732204B2 (en) * 2010-06-02 2015-06-10 株式会社流機エンジニアリング Deodorizing device and deodorizing method
US8795620B2 (en) * 2011-02-15 2014-08-05 Ati Properties, Inc. Systems and methods for recovering nitric acid from pickling solutions
WO2023127144A1 (en) * 2021-12-28 2023-07-06 カンケンテクノ株式会社 Exhaust gas purification device

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Publication number Publication date
JPH0624724U (en) 1994-04-05

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