JPS6022978B2 - Exhaust gas purification device - Google Patents

Exhaust gas purification device

Info

Publication number
JPS6022978B2
JPS6022978B2 JP51104521A JP10452176A JPS6022978B2 JP S6022978 B2 JPS6022978 B2 JP S6022978B2 JP 51104521 A JP51104521 A JP 51104521A JP 10452176 A JP10452176 A JP 10452176A JP S6022978 B2 JPS6022978 B2 JP S6022978B2
Authority
JP
Japan
Prior art keywords
exhaust gas
passage
liquid
water
gas
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
Application number
JP51104521A
Other languages
Japanese (ja)
Other versions
JPS5329275A (en
Inventor
太一 堀田
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.)
NIPPON EARO PYUURU KK
Original Assignee
NIPPON EARO PYUURU KK
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 NIPPON EARO PYUURU KK filed Critical NIPPON EARO PYUURU KK
Priority to JP51104521A priority Critical patent/JPS6022978B2/en
Publication of JPS5329275A publication Critical patent/JPS5329275A/en
Publication of JPS6022978B2 publication Critical patent/JPS6022978B2/en
Expired legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Electrostatic Separation (AREA)

Description

【発明の詳細な説明】 排ガス処理装置として各種の湿式集塵装置があるが、こ
れらの装置では微細粒子およびガス、特に水不落‘性の
ガスをよく処理しえないという欠点があり、又電気集塵
機においてもガス補集をなし得ないという欠点がある。
DETAILED DESCRIPTION OF THE INVENTION There are various types of wet dust collectors used as exhaust gas treatment equipment, but these equipment have the disadvantage that they cannot effectively treat fine particles and gases, especially water-resistant gases. Electrostatic precipitators also have the disadvantage of not being able to collect gas.

特に接着剤や塗料工場の化学工場において使用されてい
る揮発性の溶剤および可塑剤から発生する水不溶性のガ
ス、例えばベンゼントルェン、キシレン、フタル酸ジェ
ステルなどについては従来の湿式集塵機若しくは電気集
塵機を用いても除去することは困難であった。本発明は
これらの水不溶性ガスを含む排ガスの処理方法について
研究を重ねた結果、前記水不溶性ガスを予め化学的に処
理し、固体状ないしは液状、好ましくは水可溶性の微細
粒子となし、次いで帯電凝集および又は湿式処理するこ
とが有用であることを見出し本発明を完成した。
In particular, water-insoluble gases generated from volatile solvents and plasticizers used in chemical plants such as adhesives and paint factories, such as benzenetoluene, xylene, and phthalate esters, are treated with conventional wet dust collectors or electrostatic precipitators. Even if used, it was difficult to remove. As a result of repeated research on methods for treating exhaust gas containing these water-insoluble gases, the present invention has been developed by chemically treating the water-insoluble gases in advance to form them into solid or liquid, preferably water-soluble, fine particles, and then charging them. The present invention was completed by discovering that agglomeration and/or wet processing is useful.

以下本発明の実施例を図面と共に説明する。Embodiments of the present invention will be described below with reference to the drawings.

U字型排ガス通路の排ガス導入ダクト1内には排ガス中
の水不落性ガスと反応し、これを固体状ないいま液状、
好ましくは水可溶性の微細粒子に変化させる反応剤を噴
出する噴射口2,2′を設け反応部Aを形成し、その先
には碍子3を介して高鷲圧発生装置14と連結した放電
極4を設け、該放電極と排ガス通路内壁との間に高電圧
を印加しコロナ放電を起す荷電部Bを形成する。該荷電
部下方には排ガスの気液接触と洗浄液処理を行なう液槽
5を前記荷電部と接続して設け、排ガス降下通路の上部
にはノズル6を付設し、ノズルよりの噴出水は通路内壁
面を洗浄流下し液槽内に流入する。液槽5の他端はU字
型排ガス上昇通路7に接続し当該通路は内部に散水頃霧
ノズル8とェリミネーター9が設けられ洗浄部Cを形成
している。前記のノズル6,8はポンプ10を介して液
槽に連結し洗浄液が循環するようになっている。なお、
前記液槽5の側面には沈澱物および浮遊物取出し口11
を設ける。本願発明は上記の如く構成されているので排
ガスが反応部Aに導入されると噴射口2,2′より噴射
される反応剤と接触することによって、排ガスは化学変
化をおこし、固体状若しくは液状又は水溶性の液状微細
粒子に変化しつつ次の荷電部Bに導入される。なお、本
発明において使用される反応剤は気体、液体のいずれで
もよく、酸素、オゾン過酸化水素等の酸化剤、硫酸、無
水硫酸、クロロ硫酸、塩化スルフリル等のスルホン化剤
を用いることができるが、特にオゾン、無水硫酸のよう
な気体状の反応剤を用いると有利である。
In the exhaust gas introduction duct 1 of the U-shaped exhaust gas passage, the water-retaining gas in the exhaust gas reacts with the water, converting it into solid, now liquid,
Preferably, injection ports 2 and 2' for ejecting a reactant to be converted into water-soluble fine particles are provided to form a reaction section A, and beyond that a discharge electrode 4 connected to a high pressure generator 14 via an insulator 3 is provided. A charging section B is formed in which a high voltage is applied between the discharge electrode and the inner wall of the exhaust gas passage to cause corona discharge. A liquid tank 5 for gas-liquid contact of exhaust gas and cleaning liquid treatment is provided below the charging section, connected to the charging section, and a nozzle 6 is attached to the upper part of the exhaust gas descending passage, and the water jetted from the nozzle flows into the passage. The liquid washes down the wall and flows into the liquid tank. The other end of the liquid tank 5 is connected to a U-shaped exhaust gas ascending passage 7, which forms a cleaning section C with a spray nozzle 8 and an eliminator 9 provided therein. The nozzles 6 and 8 are connected to a liquid tank via a pump 10 so that the cleaning liquid is circulated therein. In addition,
A sediment and suspended matter outlet 11 is provided on the side surface of the liquid tank 5.
will be established. Since the present invention is configured as described above, when the exhaust gas is introduced into the reaction section A, the exhaust gas undergoes a chemical change by contacting the reactant injected from the injection ports 2 and 2', and becomes solid or liquid. Alternatively, the particles are introduced into the next charging section B while changing into water-soluble liquid fine particles. The reactant used in the present invention may be either gas or liquid, and oxygen, ozone, oxidizing agents such as hydrogen peroxide, and sulfonating agents such as sulfuric acid, sulfuric anhydride, chlorosulfuric acid, and sulfuryl chloride can be used. However, it is particularly advantageous to use gaseous reactants such as ozone or sulfuric anhydride.

例えば、トリェン、キシレン、等を含んだ排ガスを無水
硫酸で処理した場合、これらの水不溶性ガスは各々パラ
ー又はオルトトルェンスルホン酸およびパラー、オルト
ー、又はメタキシレンスルホン酸に変化し、水に不溶な
微細粒子となって次の工程に入り処理される。又、未反
応の無水硫酸は水との接触により液状となるので容易に
除去される。荷電部Bにおいて、排ガス中の汚染物質は
帯電し荷電部内壁に集塵されノズル6の噴出水によって
流下される。
For example, when exhaust gas containing triene, xylene, etc. is treated with anhydrous sulfuric acid, these water-insoluble gases change to para- or ortho-toluene sulfonic acid and para-, ortho-, or meta-xylene sulfonic acid, respectively, which are insoluble in water. It becomes fine particles and is processed in the next process. Furthermore, unreacted sulfuric anhydride becomes liquid upon contact with water and is therefore easily removed. In the charging section B, pollutants in the exhaust gas are charged, collected on the inner wall of the charging section, and flowed down by water jetted from the nozzle 6.

又場合により一部帯電微細粒子は凝集しつつ、排ガスと
共に液槽の液面に叩きつけられ除かれると共に排ガスは
旋回して液槽上部と気液接触しながら浄化され洗浄部C
に導入される。洗浄部では散水燈霧ノズルから出る洗浄
液と気液接触することにより排ガスは補捉浄化される。
この場合通常のスクラバーでは除去不可能な排ガス中の
汚染ガス微細汚染物質といえども、本装置においては予
め反応剤で処理し固体状又は液状微細粒子化しており、
且つ荷電部にて帯電凝集し粒子が大きくなっているので
、洗浄液による浄化も可能となり効果も大となる。浄化
された排ガスはェリミネータ9で除湿され外部に放出さ
れる。
In addition, in some cases, some of the charged fine particles are agglomerated and are struck against the liquid surface of the liquid tank together with the exhaust gas and removed, and the exhaust gas swirls and is purified while coming into gas-liquid contact with the upper part of the liquid tank in the cleaning section C.
will be introduced in In the cleaning section, the exhaust gas is captured and purified by gas-liquid contact with the cleaning liquid discharged from the water spray nozzle.
In this case, even if the fine pollutants in the exhaust gas cannot be removed with a normal scrubber, this device treats them with a reactant in advance and turns them into solid or liquid fine particles.
In addition, since the particles are charged and agglomerated in the charging section and become large, cleaning with a cleaning liquid becomes possible, and the effect becomes greater. The purified exhaust gas is dehumidified by an eliminator 9 and discharged to the outside.

なお本発明装置においてはノズル6より噴出される水が
荷電部内壁上を流下し液槽内に落下して水面12を波動
させるばかりでなく荷電部よりの旋回ガス流と対面する
水膜13を形成することとなるので排ガスとの気液接触
が促進されガス浄化に有効に作用する。なお、荷電部と
洗浄部の通路形状を逆載頭円錐型にすると洗浄が内壁に
とぎれない水膜を形成するので壁面洗浄及び排ガスとの
気液接触により効果的である。
In the device of the present invention, the water ejected from the nozzle 6 not only flows down the inner wall of the charging section and falls into the liquid tank, causing waves on the water surface 12, but also forms a water film 13 facing the swirling gas flow from the charging section. As a result, gas-liquid contact with the exhaust gas is promoted and it acts effectively on gas purification. It should be noted that if the passage shape of the charging section and the cleaning section is made into an inverted truncated conical shape, cleaning will form an uninterrupted water film on the inner wall, which will be more effective for wall surface cleaning and gas-liquid contact with the exhaust gas.

又排ガス送風に用いるファンは電離部又は洗浄部の前後
に押込み又は吸引ファンを適宜取付可能であるが液槽上
部通路内に設けると礎梓作用により液槽面と排ガスとの
気液接触により効果的である。
In addition, the fan used for blowing the exhaust gas can be pushed in or a suction fan can be installed before and after the ionization section or cleaning section, but if it is installed in the upper passage of the liquid tank, it will be more effective due to the gas-liquid contact between the liquid tank surface and the exhaust gas due to the footing effect. It is true.

本発明装置によれば、排ガス導入ダクト内に反応部を設
けることによって除去すべき汚染ガスを電気集塵若しく
は湿式集塵可能な固体状若しくは液状、好ましくは水可
溶性の微細粒子とすることによって、橘捉除去を計るほ
か排ガス処理通路がU字型に形成されているので、排ガ
スの有効な気液接触が可能で高率の排ガス浄化効果をあ
げることができる。
According to the device of the present invention, by providing a reaction part in the exhaust gas introduction duct, the contaminated gas to be removed is converted into solid or liquid, preferably water-soluble, fine particles that can be electrostatically or wet-collected. In addition to trapping and removing gas, the exhaust gas treatment passage is formed in a U-shape, allowing effective gas-liquid contact with the exhaust gas, resulting in a high rate of exhaust gas purification.

又荷電部と洗浄部を液槽上に形成しているので洗浄液の
処理及び再生循環利用も合理的に行いうる。
Furthermore, since the charging section and the cleaning section are formed on the liquid tank, the cleaning solution can be efficiently processed and recycled.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本願発明の一実施例を示す縦断面図を示す。 A…反応部、B・・・荷電部、C・・・洗浄部、2,2
′・・・噴射口、4…放電極、5・・・液槽、6・・・
ノズル、8・・・散水燈霧ノズル、9・・・ェリミネー
ター。
FIG. 1 shows a longitudinal sectional view showing an embodiment of the present invention. A...Reaction part, B...Charging part, C...Cleaning part, 2,2
'...Injection port, 4...Discharge electrode, 5...Liquid tank, 6...
Nozzle, 8... Water light fog nozzle, 9... Eliminator.

Claims (1)

【特許請求の範囲】[Claims] 1 U字型に形成した排ガス通路の排ガス導入ダクト1
内に有機溶媒系汚染ガス成分と反応する物質を噴出する
噴射口2,2′を設け、U字型排ガス降下通路は濡壁状
に形成すると共に、その内部に荷電部Bを設置し、これ
に続く通路下方底部には液槽5、排ガス上昇通路内には
洗浄部Cを設けたことを特徴とする排ガス浄化装置。
1 Exhaust gas introduction duct 1 with U-shaped exhaust gas passage
Injection ports 2 and 2' for ejecting substances that react with organic solvent-based pollutant gas components are provided inside the U-shaped exhaust gas descending passage, and a charging section B is installed inside the U-shaped exhaust gas descending passage. An exhaust gas purification device characterized in that a liquid tank 5 is provided at the lower bottom of the passage leading to the exhaust gas, and a cleaning section C is provided in the exhaust gas rising passage.
JP51104521A 1976-08-31 1976-08-31 Exhaust gas purification device Expired JPS6022978B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51104521A JPS6022978B2 (en) 1976-08-31 1976-08-31 Exhaust gas purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51104521A JPS6022978B2 (en) 1976-08-31 1976-08-31 Exhaust gas purification device

Publications (2)

Publication Number Publication Date
JPS5329275A JPS5329275A (en) 1978-03-18
JPS6022978B2 true JPS6022978B2 (en) 1985-06-05

Family

ID=14382785

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51104521A Expired JPS6022978B2 (en) 1976-08-31 1976-08-31 Exhaust gas purification device

Country Status (1)

Country Link
JP (1) JPS6022978B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012147387A1 (en) * 2011-04-28 2012-11-01 エドワーズ株式会社 Wet electric dust collector

Also Published As

Publication number Publication date
JPS5329275A (en) 1978-03-18

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