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JP2002045640A - Method and device for eliminating blue smog - Google Patents

Method and device for eliminating blue smog

Info

Publication number
JP2002045640A
JP2002045640A JP2000270793A JP2000270793A JP2002045640A JP 2002045640 A JP2002045640 A JP 2002045640A JP 2000270793 A JP2000270793 A JP 2000270793A JP 2000270793 A JP2000270793 A JP 2000270793A JP 2002045640 A JP2002045640 A JP 2002045640A
Authority
JP
Japan
Prior art keywords
liquid
foaming
main body
outer cylinder
pipe
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
Application number
JP2000270793A
Other languages
Japanese (ja)
Inventor
Koichi Nishimura
幸一 西村
Tatsuo Suzuki
達雄 鈴木
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.)
ECOTEC KK
Suzuki Shoji KK
Original Assignee
ECOTEC KK
Suzuki Shoji 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 ECOTEC KK, Suzuki Shoji KK filed Critical ECOTEC KK
Priority to JP2000270793A priority Critical patent/JP2002045640A/en
Publication of JP2002045640A publication Critical patent/JP2002045640A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y02A50/2351Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust

Landscapes

  • Separation Of Particles Using Liquids (AREA)
  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress dust such as blue smog generated in an asphalt manufacturing plant. SOLUTION: The method for eliminating the blue smog, or the like, comprises forcedly sucking oil smoke, or the like, generated in the plant into a blue smog elimination device by utilizing a negative pressure caused by a fan device provided at the rear of the blue smog elimination device, then separating the oil smoke, or the like, by the cyclone effect in the blue smog elimination device, simultaneously spraying a foamed liquid foamed by adding an air pressure to a mixed liquid of a foaming agent and a deodorant onto the oil smoke, or the like, being separated so as to collide and mix the foamed liquid with the oil smoke, or the like, and to cover the oil smoke, or the like, with the foam, separating the oil smoke, or the like, into a clear gas and a sludge material such as oil sludge, and discharging/exhausting them from the device.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、工場で発生するブ
ルースモッグとその悪臭を除去する方法とその装置に関
するものである。
[0001] 1. Field of the Invention [0002] The present invention relates to a method and an apparatus for removing bluesmog generated in a factory and its odor.

【0002】[0002]

【従来の技術】従来は、アスファルト製造工場で発生す
る油分の混じった青色がかった煙であるブルースモッグ
及びその臭の対策は、設備費が高く又ブルースモッグお
よび臭いを消す設備をしてもその設備に対する効果の期
待も薄く、現状では、工場で発生する油煙を工場の煙突
の先端に笠状覆いを設け集煙して、それをバーナー等で
燃焼させ処理していた。
2. Description of the Related Art Conventionally, measures against bluesmog, which is a bluish smoke mixed with oil generated at an asphalt manufacturing plant, and its odor have been taken at a high facility cost, and even with equipment for eliminating bluesmog and odor. There is little expectation of the effect on the equipment, and at present, oil fumes generated in factories are provided with a cap-shaped cover at the end of the chimney of the factory, collected, and burned by a burner or the like for treatment.

【0003】[0003]

【発明が解決しようとする課題】しかし、特に、臭いは
消し難く、工場周辺に隣接する地域住民より公害問題と
して騒がれ問題となっている。一方、スモッグ対策とし
て法規制が施行され、何らかの対策を考慮しなくてはな
らなくなった。工場の製造過程で発生するスモッグは工
場で対策を講じなければならない。大掛かりなスモッグ
排除装置を設置する工場もでてきたが費用も嵩みネック
となっていた。
However, in particular, the smell is difficult to eliminate, and the local residents adjacent to the factory have been making noise as a pollution problem. On the other hand, legislation was enforced as a measure against smog, and some measures had to be taken into account. Smog generated during the manufacturing process of a factory must be countered at the factory. Some factories have installed large-scale smog elimination devices, but the cost has been a bottleneck.

【0004】本発明は、上記の課題を解決するためにな
されたもので、アスファルト精製工程で発生するブルー
スモッグ等の公害物質を捕捉し、汚泥物と清浄ガスに分
離させる気液分離装置を提供することを目的とする。
The present invention has been made to solve the above-mentioned problems, and provides a gas-liquid separation device for capturing pollutants such as bluesmog generated in an asphalt refining process and separating the pollutants into sludge and clean gas. The purpose is to do.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に、請求項1記載のブルースモッグ排除方法の発明は、
サイクロン作用を有する気液分離器の本体と、本体の外
部に設けたファン装置と、発泡液供給装置と、コンプレ
ッサーとからなり、工場で発生したブルースモッグ等を
ファン装置の負圧作用により、煙道ダクトを介して本体
内に導き、一方、発泡液供給装置より水と発泡剤と消臭
剤とを混合した発泡液を液管を介して本体に導き、発泡
液は液管の中途に設けた発泡器内で、コンプレッサーの
エア圧にて液状発泡液を泡状発泡液に変え、本体内で泡
状発泡液を渦巻状に回転降下する油煙等に噴射し、油煙
等とこの泡状発泡液とを衝突混合し泡数を増加させると
共に分離しつつある油煙等の気液を包囲又は浸潤等し
て、本体内に溜めた水面とガイド面に飛沫状に叩きつ
け、水中に重質物の泡内の油煙を沈め、軽質物の泡内の
油煙とガスを水面上に浮遊させ、上方に設けたスクリー
ンを経て上部開口部より清浄ガスを排出し、本体の下方
に溜まった汚泥物を汚泥槽に排出した。
To achieve the above object, the invention of the bluesmog elimination method according to the first aspect of the present invention comprises:
It consists of a main body of a gas-liquid separator having a cyclone action, a fan device provided outside the main body, a foaming liquid supply device, and a compressor, and smokes bluesmog and the like generated in a factory by a negative pressure action of the fan device. The foaming liquid, which is a mixture of water, a foaming agent, and a deodorant, is guided from the foaming liquid supply device to the main body through a liquid pipe, and the foaming liquid is provided in the middle of the liquid pipe. In the foaming device, the liquid foaming liquid is changed to foamy foaming liquid by the air pressure of the compressor, and the foaming foaming liquid is sprayed in the main body in a spirally rotating oil fume or the like, and the oily foam and the like are foamed. The liquid and the liquid are impacted and mixed to increase the number of bubbles and surround or infiltrate the separating gas and liquid, such as oily smoke. Submerges oil fumes in the air, and brings oil fumes and gas Is Yu, the clean gas discharged from the upper opening through a screen provided above, was discharged sludge was accumulated under the body sludge tank.

【0006】請求項2記載のブルースモッグ排除装置の
発明は、本体を、略筒状ケースの下部にホッパー部を一
体に形成した外筒と、外筒の内部と所定間隔にて上下方
向に配置され、外筒側面を貫通した煙道ダクトの開口端
部を接線方向で接続した上部が有底で下端が拡開の内部
円筒と、外筒の側面を貫通し内部円筒の上部より内部に
垂下させ外筒外より導いた発泡液を側面に設けた複数の
噴射孔より内部円筒の内周面側に吹き付ける下端が閉成
のパイプ状ノズルと、内部円筒の下端と所定間隔をもっ
てホッパー部内に固定したガイド面である断面椀型の反
転皿と、外筒の下方側部に設けたホッパー部内に水を供
給する給水管と、外筒の上端よりガス等を排出する排気
ダクトと、ホッパー部の下方より水中に沈下した汚泥等
を汚泥槽に排出する吐出口とで構成したものである。
According to a second aspect of the present invention, there is provided a bluesmog removing apparatus, wherein a main body is vertically arranged at a predetermined distance from an outer cylinder having a hopper portion integrally formed at a lower portion of a substantially cylindrical case. The upper end of the flue duct penetrating through the side of the outer cylinder is connected to the open end of the flue duct in the tangential direction. A pipe-shaped nozzle with a closed lower end that sprays the foaming liquid guided from the outside of the outer cylinder to the inner peripheral surface side of the inner cylinder through a plurality of injection holes provided on the side, and is fixed in the hopper with a predetermined distance from the lower end of the inner cylinder A reversing plate having a bowl-shaped cross section as a guide surface, a water supply pipe for supplying water into a hopper provided on the lower side of the outer cylinder, an exhaust duct for discharging gas and the like from the upper end of the outer cylinder, and a hopper. Drain sludge submerged in water from below into sludge tank Which is constituted by the discharge port.

【0007】[0007]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて詳細に説明する。
Embodiments of the present invention will be described below in detail with reference to the drawings.

【0008】図1はアスファルト精製工場で発生するブ
ルースモッグを本発明のブルースモッグ排除装置に導き
汚泥物質と清浄ガスとに分離する工程を示す工程図であ
る。図2はブルースモッグ排除装置の本体内部を表わす
断面図である。図3は図2のI−Iの断面図である。図
4はパイプ状ノズルの一般断面図である。図5は図4の
パイプ状ノズルの下端のII−IIの断面図である。
FIG. 1 is a process diagram showing a process in which bluesmog generated in an asphalt refining plant is guided to a bluesmog removing device of the present invention and separated into sludge material and clean gas. FIG. 2 is a sectional view showing the inside of the main body of the bluesmog removing device. FIG. 3 is a sectional view taken along the line II of FIG. FIG. 4 is a general sectional view of a pipe-shaped nozzle. FIG. 5 is a sectional view taken along line II-II of the lower end of the pipe-shaped nozzle of FIG.

【0009】本発明のブルースモッグ排除装置Aは、工
場で発生する油煙等を、ブルースモッグ排除装置Aの後
方に配置したファン装置の負圧作用にて、ブルースモッ
グ排除装置内に強制的に吸入し、ブルースモッグ排除装
置内のサイクロン効果で油煙等を気液分離させ、更に、
分離しつつある油煙等に、発泡剤と消臭剤との混合液に
エア圧を加え発泡させた泡状発泡液を噴き付けて油煙等
を泡で包み込み、油煙等の微粒子、浮遊塵、臭いを大気
中に拡散するのを鎮め、油煙等を清浄ガスと油泥等の汚
泥物に分離させ、装置から排出させたものである。
The bluesmog elimination device A of the present invention forcibly sucks oil smoke and the like generated in a factory into the bluesmog elimination device by the negative pressure action of a fan device disposed behind the bluesmog elimination device A. The oil and smoke are separated into gas and liquid by the cyclone effect in the bluesmog elimination device.
Applying air pressure to a mixture of a foaming agent and a deodorant, and spraying a foamed foaming liquid into the separating oil fumes and the like by applying air pressure, the oil fumes and the like are wrapped in bubbles, and fine particles such as oil fumes, floating dust, and odors Is prevented from diffusing into the atmosphere, oily smoke and the like are separated into clean gas and sludge such as oily mud, and discharged from the apparatus.

【0010】以下、本発明の実施の形態を詳細に説明す
る。アスファルト製造工場の精製工程の蒸留残渣で生す
る油煙等のブルースモッグは、灰、不完全燃焼の塵の油
煙と、化学変化で発生する特殊な臭いとからなる。本発
明のブルースモッグ排除装置Aは、図2に示すように、
大きくは、外筒1と、内部円筒5と、パイプ状ノズル3
と、反転皿4と、給水管17と、ダクト12とで構成さ
れる本体Hと、本体の周囲に配設する装置等からなる
Hereinafter, embodiments of the present invention will be described in detail. Bluesmog such as oil fumes generated from the distillation residue in the asphalt manufacturing plant is composed of ash, oil fumes of incompletely combusted dust, and special odors generated by chemical changes. As shown in FIG. 2, the bluesmog elimination device A of the present invention comprises:
Largely, an outer cylinder 1, an inner cylinder 5, a pipe-shaped nozzle 3
And a main body H composed of a reversing plate 4, a water supply pipe 17, and a duct 12, a device disposed around the main body, and the like.

【0011】まず、本体Hの周囲に配設する装置等を説
明する。装置は以下のものである。本体Hの外筒1の側
部には、工場20側から煙道ダクト11が導かれ、又、
発泡剤等の発泡液供給装置26から液状発泡液Lが発泡
器27にてコンプレッサー28からのエア圧が加わり泡
状となった泡状発泡液Fが液管13を介して導かれ、更
に、外筒1の下方側部には、給水管17が導かれ、本体
Hの排気ダクト12の後工程には、負圧作用で煙道ダク
ト11から油煙等を強制的に引き込み排気ダクト12か
ら排気させるファン装置19が設けられている。ファン
装置19はターボファンであるが、プレートファンでも
よい。又、ホッパー部2の底部の吐出口21と連結し排
管31を介して、排水を溜める汚泥槽15が配置されて
いる。
First, a device disposed around the main body H will be described. The equipment is as follows. A flue duct 11 is guided to the side of the outer cylinder 1 of the main body H from the factory 20 side.
A liquid foaming liquid L is supplied from a foaming liquid supply device 26 such as a foaming agent by a foaming device 27, and an air pressure from a compressor 28 is applied thereto. A water supply pipe 17 is guided to the lower side of the outer cylinder 1, and in a subsequent process of the exhaust duct 12 of the main body H, oil smoke or the like is forcibly drawn from the flue duct 11 by a negative pressure action and exhausted from the exhaust duct 12. A fan device 19 is provided. The fan device 19 is a turbo fan, but may be a plate fan. Further, a sludge tank 15 for storing drainage is disposed via a discharge pipe 31 which is connected to the discharge port 21 at the bottom of the hopper section 2.

【0012】次に、本体Hの構造を説明する。本体Hは
図に示すように、工場20の天井側の上部に設けた煙道
ダクト11を介して油煙等Sを導かれ、アスファルト製
造工場に隣接して架台25を介して設置するもので、地
上から外筒の頂部までは5メートル程の高さを有する。
Next, the structure of the main body H will be described. As shown in the figure, the main body H is configured such that oil smoke and the like S are guided through a flue duct 11 provided on the ceiling side of a factory 20 and installed via a pedestal 25 adjacent to an asphalt manufacturing factory. It has a height of about 5 meters from the ground to the top of the outer cylinder.

【0013】本体Hの外筒1は、上部は略筒状で下方は
油煙等と泡を混合させるため筒状より若干膨れた筒状を
有し、下部のホッパー部2は漏斗状で下端に吐出口21
を有する。ホッパー部2には、センサー32が設けら
れ、ホッパー部2に自然沈降した重質物の溜り具合を検
知し、排管31の中途に設けたポンプ30を駆動して重
質物Oを抜き取る。ホッパー部2から重質物Oを抜き取
る方法は、上記のセンサー方式の他に、タイマー方式も
ある。タイマー方式の場合は、ポンプ30に予め泥澱時
間を測っておいて,その時間をタイマーセットして順次
繰り返しポンプを駆動して重質物Oを抜き取るものであ
る。
The outer cylinder 1 of the main body H has a substantially cylindrical upper part and a slightly lower cylindrical part for mixing oil smoke and the like with the lower part. The lower hopper part 2 has a funnel-like shape at the lower end. Discharge port 21
Having. The hopper section 2 is provided with a sensor 32, which detects the state of accumulation of the heavy matter spontaneously settling in the hopper section 2 and drives the pump 30 provided in the middle of the discharge pipe 31 to remove the heavy matter O. As a method of extracting the heavy material O from the hopper section 2, there is a timer method in addition to the above-described sensor method. In the case of the timer method, the sludge time is measured in advance in the pump 30, and the time is set on a timer, and the pump is sequentially and repeatedly driven to remove the heavy material O.

【0014】内部円筒5は、外筒1の内部と所定間隔に
て上下方向に配置され、上部有底の筒を倒設させ、下端
部は拡開したガイド部6を形成して外筒1内に固定され
ている。内部円筒5の上方周面には、外筒1の上部周面
を貫通した煙道ダクト11を接線状に接続するように吸
入口9を形成している。吸入口9が内部円筒5に接線上
に接続しているのは、煙道ダクト11から流れてくる油
煙等Sの流体を内部円筒5内で旋回して降下させ、遠心
力と重力を利用して流体中の微粒子を分離させるため
で、公知のサイクロンである。
The inner cylinder 5 is vertically arranged at a predetermined interval from the inside of the outer cylinder 1, the upper cylinder having a bottom is inverted, and the lower end forms an expanded guide portion 6 to form the outer cylinder 1. Is fixed inside. An intake port 9 is formed on the upper peripheral surface of the inner cylinder 5 so as to tangentially connect a flue duct 11 penetrating the upper peripheral surface of the outer cylinder 1. The reason why the suction port 9 is tangentially connected to the inner cylinder 5 is that the fluid such as the oil smoke flowing from the flue duct 11 is swirled and lowered in the inner cylinder 5 by utilizing centrifugal force and gravity. It is a known cyclone for separating fine particles in a fluid.

【0015】内部円筒5の下方には、内部円筒5の下端
と所定間隔をもって円筒下部又はホッパー部2内に固定
したガイド面である断面椀型の反転皿4が設けられてい
る。又、同じく、内部円筒5の下方周面の全周には、反
転皿からの油煙、浮遊塵、臭い等と反応湿潤した密着気
泡を反転させるガイド面である抑流部7が設けられてい
る。反転皿4で、泡状の気体が液体内に叩きつけられ飛
沫となって気液体が混合され、飛沫の勢い(衝撃)で混
合した泡状発泡液が反転皿4の側面4cで反転し、更の
抑流部7で反転して気液体を包む泡状発泡液の泡立ちを
更に助勢されるようにしている。反転皿4の底面4a
は、パンチングプレート4bで出来ており,水の出入が
自由である。外筒1の中間位置には、メッシュのスクリ
ーン8が内周に沿って設けられ泡fが上方のダクトに流
れ出ないようにしている。
Below the inner cylinder 5, there is provided a reversing plate 4 having a bowl-shaped cross section, which is a guide surface fixed in the lower portion of the cylinder or in the hopper 2 at a predetermined distance from the lower end of the inner cylinder 5. Similarly, the entire periphery of the lower peripheral surface of the inner cylinder 5 is provided with a flow restricting portion 7 which is a guide surface for reversing the contact bubbles that have wetted by reacting with oil smoke, floating dust, odor and the like from the reversing plate. . In the reversing plate 4, the foamy gas is smashed into the liquid to form droplets and the gas-liquid is mixed, and the foamed foamed liquid mixed by the force of the droplets (impact) is reversed on the side surface 4c of the reversing plate 4, and The bubbling of the foamed liquid wrapping the gaseous liquid by reversing at the squeezing section 7 is further assisted. Bottom 4a of reversing plate 4
Is made of a punching plate 4b, and water can freely enter and exit. At an intermediate position of the outer cylinder 1, a mesh screen 8 is provided along the inner periphery to prevent the bubbles f from flowing out to the upper duct.

【0016】内部円筒5の上底部からは、発泡液の液管
13と連通し、外筒1の上部周面を貫通し折曲して、更
に、内部円筒5を貫通した細径のパイプ状ノズル3が内
部に導かれている。このパイプ状ノズル3は内部円筒5
の上底で固定されている。パイプ状ノズル3は、その周
面側には、図に示すように、内部円筒5の内面の周方向
に吹き付ける複数の噴出孔10を有し、各噴出孔10の
周面側にはソケット18を溶接し、固定したソケット1
8に設けた貫通の螺子孔に発泡ノズル14を捩じ込む。
発泡ノズル14にはパイプ状ノズル3内に流れてくる泡
状発泡液Fを発泡ノズル14のノズル孔から内部円筒5
側に拡散し噴出す。噴出孔10は同周面に3個設け、各
上下の噴出孔10の間隔は所定の間隔で設ける。パイプ
状ノズル3の下端の開口部3aには、図5に示すよう
に、プラグ盲栓32を捩じ込んでいる。
From the upper bottom of the inner cylinder 5, it communicates with the liquid pipe 13 of the foaming liquid, penetrates the upper peripheral surface of the outer cylinder 1, bends, and further forms a small-diameter pipe penetrating the inner cylinder 5. The nozzle 3 is guided inside. This pipe-shaped nozzle 3 has an inner cylinder 5
It is fixed at the upper bottom. As shown in the figure, the pipe-shaped nozzle 3 has a plurality of ejection holes 10 for spraying in the circumferential direction of the inner surface of the inner cylinder 5 on the peripheral surface side, and a socket 18 on the peripheral surface side of each ejection hole 10. And fixed socket 1
The foaming nozzle 14 is screwed into the threaded through-hole provided at 8.
The foaming nozzle 14 is supplied with the foaming foaming liquid F flowing into the pipe-shaped nozzle 3 through the nozzle hole of the foaming nozzle 14.
Spreads out to the side. The three orifices 10 are provided on the same peripheral surface, and the intervals between the upper and lower orifices 10 are provided at predetermined intervals. A plug blind plug 32 is screwed into the opening 3a at the lower end of the pipe-shaped nozzle 3, as shown in FIG.

【0017】パイプ状ノズル3へは、発泡剤と消臭剤2
2と水23とを混合させた液状発泡液Lに、発泡器27
内で、更に、コンプレッサー28のエア圧が加わり泡状
となった泡状発泡液Fが送り込まれる。発泡剤の薬液と
消臭剤は、支管23b、22b、24bの途中に設けた
パルスポンプ(ダイヤフラムポンプ)にて強制的に液管
13に送り込まれる。発泡液Fは、本体Hから離れた場
所に設置した発泡用の発泡液供給装置26から供給す
る。この例では離れているが本体H近傍又は本体Hに組
み込んでもよい。発泡液供給装置26は、図1に示すよ
うに、水槽23と、薬液である発泡剤槽22と、消臭剤
槽24とからなる。水槽23に設ける水ポンプ23a
は、2段高圧ポンプ(流速は秒速0.833メートル、
揚程32メートル)を使用する。発泡剤槽22と、消臭
剤槽24は、パルスポンプ(ダイヤフラムポンプ)22
a、24aが設けられ、水ポンプの支管23bの流速
で、支管22b、24bから強制的に液管13に送り込
まれ発泡器に混合液が送り込まれる。尚、各支管22
b、23b、24bには、各槽から引出す液が逆戻りし
ないように逆止弁22c、23c、24cがそれぞれ設
けられている。
A blowing agent and a deodorant 2 are supplied to the pipe-shaped nozzle 3.
2 and water 23 are mixed with a liquid foaming liquid L,
Further, the foamed foaming liquid F which is foamed by the air pressure of the compressor 28 is further fed therein. The liquid chemical of the foaming agent and the deodorant are forcibly fed into the liquid pipe 13 by a pulse pump (diaphragm pump) provided in the middle of the branch pipes 23b, 22b, 24b. The foaming liquid F is supplied from a foaming liquid supply device 26 for foaming installed at a location away from the main body H. In this example, they are separated from each other, but they may be incorporated in the vicinity of or in the main body H. As shown in FIG. 1, the foaming liquid supply device 26 includes a water tank 23, a foaming agent tank 22 as a chemical, and a deodorant tank 24. Water pump 23a provided in water tank 23
Is a two-stage high-pressure pump (flow rate is 0.833 meters per second,
Use a lift of 32 meters). The foaming agent tank 22 and the deodorant tank 24 include a pulse pump (diaphragm pump) 22.
a and 24a are provided, and at a flow rate of the branch pipe 23b of the water pump, the branch pipes 22b and 24b are forcibly fed into the liquid pipe 13 and the mixed liquid is fed to the foaming device. In addition, each branch pipe 22
Check valves 22c, 23c, and 24c are provided in b, 23b, and 24b, respectively, so that the liquid drawn from each tank does not return.

【0018】液状発泡液Lは、水と、薬液である発泡剤
22と、消臭剤24とからなる。薬液である発泡剤は、
起泡力が大で、泡沫安定度の高い薬剤を用いる。発泡剤
は、合成界面活性剤であるα−オレフィンスルホン酸塩
(AOS)を基剤(99.9パーセント)とし、その他
に起泡剤、泡強化剤、安定剤を使用する。消臭剤は、エ
ポリオンN6C又はN7Cを使用する。
The liquid foaming liquid L comprises water, a foaming agent 22 as a chemical, and a deodorant 24. The foaming agent, which is a chemical,
Use a drug with high foaming power and high foam stability. The foaming agent is based on α-olefin sulfonate (AOS), which is a synthetic surfactant, (99.9%), and further uses a foaming agent, a foam enhancer, and a stabilizer. Eporion N6C or N7C is used as a deodorant.

【0019】次に、本発明のブルースモッグ排除装置A
の作用を説明する。工場20で発生したブルースモッグ
等の油煙等Sは、装置Aの下流に設けたファンであるタ
ーボファン19の負圧作用にて、煙道ダクト11から外
筒1内の内部円筒5の吸入口9を経て内部円筒5の接線
方向に浸入し、油煙等は内部円筒5内を渦状に巻き込み
ながら降下して流れ込む(サイクロン)。この場合、内
部円筒の内面外側は内面内側に比し流速が速い。油煙等
Sは遠心力と重力にて重質物は内部円筒5の内壁に押し
付けられ軽質物と分離しながら下りて行く。その場合、
中心部は低圧となる。重質物は10μ以上の物質、軽質
物は10μ以下の物質である。
Next, the bluesmog removing device A of the present invention
The operation of will be described. Oil S such as bluesmog generated at the factory 20 is sucked from the flue duct 11 to the inner cylinder 5 in the outer cylinder 1 by the negative pressure of the turbofan 19 which is a fan provided downstream of the apparatus A. The oil and smoke and the like enter the tangential direction of the inner cylinder 5 through the pipe 9 and fall down while flowing in the inner cylinder 5 while swirling (cyclone). In this case, the flow velocity on the inner surface outside of the inner cylinder is faster than that on the inner surface inside. Heavy matter such as oily smoke S is pressed against the inner wall of the inner cylinder 5 by centrifugal force and gravity, and descends while separating from light matter. In that case,
The center is low pressure. A heavy substance is a substance of 10 μ or more, and a light substance is a substance of 10 μ or less.

【0020】一方、泡剤、消臭剤を混合した液状発泡液
Lを発泡器27内でエア圧にて泡状発泡液Fとし、水ポ
ンプ23aの圧力と、コンプレッサー28によるエア圧
とにより泡状発泡液Fをパイプ状ノズル3の各噴射孔1
0に設けた発泡ノズル14から拡散状に噴射し、泡状発
泡液Fを内部円筒5の内壁に衝突させ(衝撃)て泡fを
更に増加させる。泡fは渦を巻きながら下方に降下する
油煙等Sと交差して、油煙等の微粒子、浮遊塵、臭いに
衝突混合し付着して湿潤し、又は包囲し、飛沫となって
下方の漲った水面に衝突して泡の一部が破れ、更に泡の
増加を助勢し、泡内の微粒子の重質物は水内に浸入して
溶け、汚泥物として沈澱する。その他は、飛沫でガイド
面である反転皿の側面4cにて空中内に跳ね返され上方
の同じくガイド面である抑流部7に当たり、更に向きを
変え、水面にて再び跳ね返され、当たる毎に泡数を増加
させていく。再三、衝撃を与えて泡に圧力を加え、泡を
変形して泡内の油煙の気液分離を助勢させる。上方のフ
イルターであるスクリーン8で泡の上昇は抑えられ、ス
クリーン8を通過した泡を有しない清浄ガスG、一部の
水蒸気等は排気ダクト12を介してファン装置19の出
口19aより排出される。多くの泡fは、内部にガス、
臭、油煙の微粒子、気体中に浮遊する微粒子(塵)が入
り込み気泡を形成する。そして、外筒1内スクリーン8
下に停留する。泡fは密着気泡で起泡力も大きく、泡沫
安定度も高い。気泡の大きさは一定でなく多様である。
発泡剤と消臭剤を含む発泡液で形成される発泡液は、密
着気泡で通常切断し難く、剥がれ難い。従って、ガス、
臭い、油煙微粒子、浮遊微粒子、が、一旦、泡内に閉じ
込められ、気泡を形成すると、気泡は密着気泡で泡同士
は分離し難く大気内に油煙等の漏れる虞がない。泡は約
10時間も維持する。泡が消失したときは内部の物質
は、泡に付着していた微粒子とガスとして出る。ガス、
臭については、物質が、泡の内部で泡内に湿潤し、又、
泡の発泡剤に反応し酸化、中性化、分解等の化学反応を
繰り返し、ガス、臭は清浄ガスとして排出され、重質物
の微粒子は水内に落ち、泡が消失し汚泥物となって汚泥
槽内に沈澱する。軽質物の微粒子は泡状で空中を彷徨い
上昇する。
On the other hand, a liquid foaming liquid L mixed with a foaming agent and a deodorant is converted into a foaming foaming liquid F by an air pressure in a foaming device 27, and the foaming is performed by the pressure of a water pump 23a and the air pressure of a compressor 28. Injection liquid 1 of the pipe-shaped nozzle 3
The foamed foaming liquid 14 is ejected in a diffusing manner from the foaming nozzle 14 provided at the position 0, and the foamed foaming liquid F collides with the inner wall of the inner cylinder 5 (impact) to further increase the foam f. The foam f intersects with the oil smoke S descending downward while swirling, and impacts and mixes with fine particles such as oil smoke and the like, floating dust, and odor, and adheres, wets, or surrounds, and forms a droplet, which rises downward. A part of the foam is broken by colliding with the surface of the water, which further promotes the increase of the foam, and the heavy matter of the fine particles in the foam penetrates into the water and melts, and precipitates as sludge. Others are splashed back into the air on the side face 4c of the reversing plate, which is the guide surface, and hit the upstream restraint section 7, which is also the guide surface. Increase the number. Repeatedly, a shock is applied to the foam to apply pressure to the foam, thereby deforming the foam and assisting gas-liquid separation of the oily smoke in the foam. The rising of the bubbles is suppressed by the screen 8 which is the upper filter, and the clean gas G and a part of the water vapor, etc., which do not have the bubbles passing through the screen 8, are discharged from the outlet 19a of the fan device 19 through the exhaust duct 12. . Many bubbles f have gas,
Fine particles of odor, oily smoke, and fine particles (dust) floating in gas enter to form bubbles. And the outer cylinder 1 inner screen 8
Stop below. The foam f is a close contact foam and has a high foaming power and a high foam stability. The size of the bubbles is not constant but varies.
A foaming liquid formed from a foaming liquid containing a foaming agent and a deodorant is usually difficult to cut and peel off due to close contact bubbles. Therefore, the gas,
Once the odor, oily smoke fine particles, and floating fine particles are once trapped in the bubbles to form bubbles, the bubbles are in close contact with each other and the bubbles are difficult to separate from each other, and there is no risk of oily smoke and the like leaking into the atmosphere. The foam is maintained for about 10 hours. When the foam disappears, the substance inside comes out as fine particles and gas adhering to the foam. gas,
As for the odor, the substance gets wet inside the foam inside the foam and
Reacts with the foaming agent of the foam and repeats chemical reactions such as oxidation, neutralization, decomposition, etc., gas and odor are discharged as clean gas, heavy particulates fall into the water, bubbles disappear and sludge becomes Settles in the sludge tank. The fine particles of light matter are foamy and wander in the air to rise.

【0021】又、外筒1のホッパー部2から泡が消失し
沈澱した汚泥物は、定期的に吐出口から排管31を介し
て汚泥槽15に排水する。ホッパー部2から排出する汚
泥物は、図示しない分級器にて大きさの異なる微粒子を
流体内で沈降速度の差を利用して分離させてもよい。
尚、給水管17の水は、この装置Aの稼動中は自動的に
補水する。又、水位調整器16はチェックバルブ等でブ
ルースモッグ除去装置の水面の高さを調整するものであ
る。
The sludge from which bubbles have disappeared and settled out of the hopper portion 2 of the outer cylinder 1 is periodically drained from the discharge port to the sludge tank 15 via the discharge pipe 31. The sludge discharged from the hopper 2 may be separated by a classifier (not shown) by using fine particles having different sizes in the fluid by using a difference in sedimentation speed.
The water in the water supply pipe 17 is automatically replenished during the operation of the device A. The water level adjuster 16 adjusts the height of the water surface of the bluesmog removing device with a check valve or the like.

【0022】[0022]

【発明の効果】本発明は上記構成を有するので、下記の
効果を奏する。
Since the present invention has the above-described structure, the following effects can be obtained.

【0023】ブルースモッグと臭いを発泡剤、消臭剤の
混合して発泡させた泡内に入れ抑えるので、外気を汚さ
ない。公害対策に最適である。
Since the bluesmog and the odor are suppressed in the foam formed by mixing the foaming agent and the deodorant, the outside air is not polluted. Ideal for pollution control.

【0024】大量のブルースモッグを比較的少量の泡で
抑えることができ、二次公害もなく、経済的である。
A large amount of bluesmog can be suppressed with a relatively small amount of foam, and is economical without secondary pollution.

【0025】設備も単純で設備費用も少なく抑えられ
る。
The equipment is simple and the equipment cost can be reduced.

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

【図1】本発明のブルースモッグ除去する方法の流れ図
である。
FIG. 1 is a flowchart of a method for removing bluesmog according to the present invention.

【図2】ブルースモッグ除去装置を示す一般断面図であ
る。
FIG. 2 is a general sectional view showing a bluesmog removing apparatus.

【図3】図2のI−I断面図である。FIG. 3 is a sectional view taken along the line II of FIG. 2;

【図4】パイプ状ノズルの端部の一般断面図である。FIG. 4 is a general sectional view of an end of a pipe-shaped nozzle.

【図5】図4のII−II断面図である。FIG. 5 is a sectional view taken along line II-II of FIG.

【符号の説明】[Explanation of symbols]

A ブルースモッグ排除装置 H 本体 S 油煙等 L 液状発泡液 F 泡状発泡液 G 清浄ガス O 重質物 W 水 f 泡 1 外筒 2 ホッパー部 3 パイプ状ノズル 3a 端部 4 反転皿 5 内部円筒 6 ガイド部 7 抑流部 8 スクリーン 9 吸入口 10 噴射孔 11 煙道ダクト 12 排気ダクト 13 液管 14 ソケット 15 汚泥槽 16 水位調整器 17 給水管 18 発泡ノズル 19 ファン装置 19a 吹出口 20 工場 21 吐出口 22 発泡剤槽 22a ポンプ 23 水槽 24 消臭剤槽 25 架台 26 発泡液供給装置 27 発泡器 28 コンプレッサー 29 エアホース 30 ポンプ 31 排管 32 プラグ盲栓 A Blue Smog Elimination Device H Main Body S Oily Smoke L Liquid Foaming Liquid F Foamed Foaming Liquid G Clean Gas O Heavy Material W Water f Foam 1 Outer Cylinder 2 Hopper 3 Pipe Nozzle 3a End 4 Reversing Plate 5 Inner Cylinder 6 Guide Part 7 Suppression part 8 Screen 9 Suction port 10 Injection hole 11 Flue duct 12 Exhaust duct 13 Liquid pipe 14 Socket 15 Sludge tank 16 Water level adjuster 17 Water supply pipe 18 Foaming nozzle 19 Fan device 19a Blow outlet 20 Factory 21 Discharge port 22 Foaming agent tank 22a Pump 23 Water tank 24 Deodorant tank 25 Stand 26 Foaming liquid supply device 27 Foamer 28 Compressor 29 Air hose 30 Pump 31 Drainage 32 Plug blind plug

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 47/04 53/77 Fターム(参考) 4D002 AA40 AB02 BA02 BA16 CA01 CA04 DA35 DA64 DA70 EA13 HA01 4D032 AA02 AC03 AC09 AE01 BA03 BA06 BB18 DA01 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B01D 47/04 53/77 F-term (Reference) 4D002 AA40 AB02 BA02 BA16 CA01 CA04 DA35 DA64 DA70 EA13 HA01 4D032 AA02 AC03 AC09 AE01 BA03 BA06 BB18 DA01

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 サイクロン作用を有する気液分離器の本
体と、本体の外部に設けたファン装置と、発泡液供給装
置と、コンプレッサーとからなり、工場で発生したブル
ースモッグ等をファン装置の負圧作用により、煙道ダク
トを介して本体内に導き、一方、発泡液供給装置より水
と発泡剤と消臭剤とを混合した発泡液を液管を介して本
体に導き、発泡液は液管の中途に設けた発泡器内で、コ
ンプレッサーのエア圧にて液状発泡液を泡状発泡液に変
え、本体内で泡状発泡液を渦巻状に回転降下する油煙等
に噴射し、油煙等とこの泡状発泡液とを衝突混合し泡数
を増加させると共に分離しつつある油煙等の気液を包囲
又は浸潤等して、本体内に溜めた水面とガイド面に飛沫
状に叩きつけ、水中に重質物の泡内の油煙を沈め、軽質
物の泡内の油煙とガスを水面上に浮遊させ、上方に設け
たスクリーンを経て排気ダクトより清浄ガスを排出し、
本体の下方に溜まった汚泥物を汚泥槽に排出したことを
特徴とするブルースモッグ排除方法。
The apparatus comprises a main body of a gas-liquid separator having a cyclone action, a fan device provided outside the main body, a foaming liquid supply device, and a compressor. By pressure action, it is led into the main body through a flue duct, while a foaming liquid obtained by mixing water, a foaming agent and a deodorant from a foaming liquid supply device is guided to the main body through a liquid pipe, and the foaming liquid is a liquid. In the foaming device provided in the middle of the pipe, the liquid foaming liquid is changed to foamy foaming liquid by the air pressure of the compressor, and the foaming foaming liquid is sprayed into the spiral smoke that descends in the spiral in the main body, and the oily smoke, etc. This foamy foam liquid is colliding and mixed to increase the number of bubbles and surround or infiltrate the gas liquid such as oil fumes that are being separated, and splatter splashes on the water surface and the guide surface stored in the main body, and Submerge the oil smoke in the foam of the heavy material, and the oil smoke and gas in the foam of the light material. Floats on the water surface, discharges clean gas from the exhaust duct through the screen provided above,
A method for eliminating bluesmog, wherein the sludge accumulated under the main body is discharged into a sludge tank.
【請求項2】 本体を、略筒状ケースの下部にホッパー
部を一体に形成した外筒と、外筒の内部と所定間隔にて
上下方向に配置され、外筒側面を貫通した煙道ダクトの
吸入口を接線方向で接続し上部が有底で下端が拡開の内
部円筒と、外筒の側面を貫通し内部円筒の上部より内部
に垂下させ外筒外より導いた発泡液を側面に設けた複数
の噴射孔より内筒の内周面に吹き付ける下端が閉成のパ
イプ状ノズルと、内部円筒の下端と所定間隔をもってホ
ッパー部内に固定したガイド面である断面椀型の反転皿
と、外筒の下方側部に設けたホッパー部内に水を供給す
る給水管と、外筒の上端よりガス等を排出する排気ダク
トと、ホッパー部の下方より水中に沈下した汚泥物を排
出する吐出口とで構成したことを特徴とするブルースモ
ッグ排除装置。
2. An outer cylinder having a main body integrally formed with a hopper at a lower portion of a substantially cylindrical case, and a flue duct which is vertically disposed at a predetermined interval from the inside of the outer cylinder, and penetrates a side surface of the outer cylinder. Tangentially connected to each other, an inner cylinder with a bottom at the top and an expanded bottom at the bottom, and penetrates the side of the outer cylinder and hangs down from the top of the inner cylinder to the inside, and the foaming liquid guided from the outside of the outer cylinder to the side A pipe-shaped nozzle having a closed lower end for blowing the inner peripheral surface of the inner cylinder from the plurality of injection holes provided, and a reversing dish having a bowl-shaped cross section that is a guide surface fixed in the hopper with a predetermined interval from the lower end of the inner cylinder, A water supply pipe that supplies water into the hopper provided on the lower side of the outer cylinder, an exhaust duct that discharges gas and the like from the upper end of the outer cylinder, and a discharge port that discharges sludge submerged in water from below the hopper. And a bluesmog elimination device.
JP2000270793A 2000-08-04 2000-08-04 Method and device for eliminating blue smog Pending JP2002045640A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000270793A JP2002045640A (en) 2000-08-04 2000-08-04 Method and device for eliminating blue smog

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000270793A JP2002045640A (en) 2000-08-04 2000-08-04 Method and device for eliminating blue smog

Publications (1)

Publication Number Publication Date
JP2002045640A true JP2002045640A (en) 2002-02-12

Family

ID=18757171

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000270793A Pending JP2002045640A (en) 2000-08-04 2000-08-04 Method and device for eliminating blue smog

Country Status (1)

Country Link
JP (1) JP2002045640A (en)

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JP2012120720A (en) * 2010-12-09 2012-06-28 Iwao Hishida Method and device for cleaning air
CN102641659A (en) * 2011-02-22 2012-08-22 贵州中烟工业有限责任公司 Smoke gas desulfuration dust remover
KR101391149B1 (en) * 2012-08-06 2014-05-27 한성엔지니어링 주식회사 Wet scrubber
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