JPS63107727A - Gas cleaning apparatus - Google Patents

Gas cleaning apparatus

Info

Publication number
JPS63107727A
JPS63107727A JP61253916A JP25391686A JPS63107727A JP S63107727 A JPS63107727 A JP S63107727A JP 61253916 A JP61253916 A JP 61253916A JP 25391686 A JP25391686 A JP 25391686A JP S63107727 A JPS63107727 A JP S63107727A
Authority
JP
Japan
Prior art keywords
malodorous
adsorbing
gas
eliminator
chamber
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.)
Granted
Application number
JP61253916A
Other languages
Japanese (ja)
Other versions
JPH0228373B2 (en
Inventor
Tamotsu Kubota
久保田 保
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.)
SHINTOU DASUTOKOREKUTAA KK
Original Assignee
SHINTOU DASUTOKOREKUTAA 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 SHINTOU DASUTOKOREKUTAA KK filed Critical SHINTOU DASUTOKOREKUTAA KK
Priority to JP61253916A priority Critical patent/JPH0228373B2/en
Publication of JPS63107727A publication Critical patent/JPS63107727A/en
Publication of JPH0228373B2 publication Critical patent/JPH0228373B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

PURPOSE:To surely deodorize malodorous gas by a single apparatus, by dividing the interior of a casing of which the bottom part is set to a liquid sump part into a wet scrubbing chamber provided with a venturi scrubber and a dry adsorbing chamber equipped with a specific adsorbing filter material by a partition wall having an eliminator mounted to the lower part thereof. CONSTITUTION:The malodorous gas sent in from an inlet 6 passes through the gaps between the rod-shaped bodies 11 arranged in the vicinity of the venturi scrubber 13 in a wet scrubbing chamber 7 at a high speed. At this time, the absorbing solution injected from an upper spray nozzle is formed into a large amount of liquid droplets and the malodorous components in the malodorous gas are absorbed by said liquid droplets. Subsequently, the liquid droplets pass through an eliminator 4 while impinging against the zigzag wall surface thereof and fall to a lower liquid sump part 2. Further, the gas containing a very small amount of malodorous components passing through the eliminator 4 is introduced into a dry adsorbing chamber 9 and passes through an adsorbing filter material 15 to adsorb and collect the malodorous components. The adsorbing filter material 15 is formed by folding a cloth like (paper like) absorbing material into a cylindrical shape having a chrysanthemum like cross-section and has a large adsorbing area.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は悪臭ガス中の悪臭成分の吸収を行わせるために
用いられるガス清浄装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a gas cleaning device used for absorbing malodorous components in malodorous gas.

(従来の技術) 一般に悪臭ガスは極めて希薄な濃度でも臭気として感じ
られるため、通常の公害対策としては湿式洗浄装置によ
って大部分の悪臭成分を除去したうえで更に別に設けた
乾式吸着装置中の乾式吸着剤により残りの悪臭成分を吸
着させるのが普通であった。しかしこのように湿式洗浄
装置と乾式吸着装置とをそれぞれ別個に設けることは設
備費がかさむ欠点があった。また悪臭ガスが間歇的に発
生するような場合には吸着保持能を前提とした吸着剤の
所要量は少なくてもよいのであるが、ガス流の短絡を防
止するためには充填層の厚さを厚くしなければならず、
吸着剤の&8量を一定としたまま充填層の厚さを増加さ
せるとガスの通過断面積が小さくなって圧力損失が増加
するため、結局ガスの通過断面積と充填層の厚さをとも
に十分に取る必要上から吸着保持能に見合った吸着剤の
数十倍の吸着剤を充填しなければならないという欠点も
あった。
(Prior technology) Generally, malodorous gases can be perceived as an odor even at extremely dilute concentrations, so the usual pollution countermeasure is to remove most of the malodorous components using a wet cleaning device, and then dry cleaning in a separate dry adsorption device. It was common practice to adsorb the remaining malodorous components with an adsorbent. However, providing the wet cleaning device and the dry adsorption device separately in this way has the drawback of increasing equipment costs. In addition, in cases where foul-smelling gas is generated intermittently, the amount of adsorbent required may be small based on the adsorption and retention capacity, but in order to prevent short circuits in the gas flow, the thickness of the packed bed must be must be made thicker,
If the thickness of the packed bed is increased while the amount of adsorbent is kept constant, the gas passage cross-sectional area will become smaller and the pressure loss will increase. There was also the drawback that the amount of adsorbent needed to be filled was several tens of times that of the amount of adsorbent commensurate with the adsorption and retention capacity.

(発明が解決しようとする問題点) 本発明は上記のような従来の問題点を解決して、悪臭ガ
ス中の悪臭成分を1台で吸収させることができ、また必
要以上に多量の吸着剤を用いる必要のないガス清浄装置
を目的として完成されたものである。
(Problems to be Solved by the Invention) The present invention solves the above-mentioned conventional problems, and can absorb malodorous components in malodorous gas with a single unit. It was completed with the aim of creating a gas cleaning device that does not require the use of gas.

(問題点を解決するための手段) 本発明は底部を液溜部としたケーシングの内部を、下部
に邪魔板状のエリミネータを備えた隔壁によってベンチ
ュリースクラバを備えた湿式洗浄室と、布状もしくは紙
状の吸着材を断面菊花状の円筒形状に折りたたんだ吸着
濾材を備えた乾式吸着室とに区画したことを特徴とする
ものである。
(Means for Solving the Problems) The present invention provides a wet cleaning chamber equipped with a Venturi scrubber and a cloth-like or It is characterized by being divided into a dry adsorption chamber equipped with an adsorption filter material made of a paper-like adsorbent folded into a cylindrical shape with a chrysanthemum-like cross section.

(実施例) 次に本発明を図示の実施例について詳細に説明すると、
(1)は底部を液溜部(2)としたケーシングであり、
該液溜部、(2)には悪臭成分の吸収液が所定の液面高
さまで注入弁(3)から供給されている。このケーシン
グ(1)の内部は下部にエリミネータ(4)を備えた隔
壁(5)によって入口(6)側の湿式洗浄室(7)と出
口(8)側の乾式吸着室(9)とに区画されている。エ
リミネータ(4)は図示のように屈曲した流路を形成す
る断面ジグザグ状の邪魔板を平行に配置したものであり
、紙面の前後方向にわずかな傾斜を持たせである。また
エリミネータ(4)の最下部は垂下部Qlとされて液溜
部(2)の液面下に浸漬されている。
(Example) Next, the present invention will be explained in detail with reference to the illustrated example.
(1) is a casing with a liquid reservoir (2) at the bottom;
A malodorous component absorbing liquid is supplied to the liquid reservoir (2) from an injection valve (3) up to a predetermined liquid level. The inside of this casing (1) is divided into a wet cleaning chamber (7) on the inlet (6) side and a dry adsorption chamber (9) on the outlet (8) side by a partition wall (5) with an eliminator (4) at the bottom. has been done. As shown in the figure, the eliminator (4) has baffle plates with a zigzag cross section arranged in parallel to form a curved flow path, and is slightly inclined in the front-rear direction of the paper. The lowest part of the eliminator (4) is a hanging part Ql and is immersed below the liquid level of the liquid reservoir (2).

湿式洗浄室(7)には例えば断面が円形、楕円形もしく
は多角形の複数の棒状体(11)を平行に近接配置して
棒状体(11)の相互間の間隙をベンチュリーとすると
ともに、その上方にスプレーノズル(12)を配置した
ベンチュリースクラバ(13)が設けられている。スプ
レーノズル(12)には循環ポンプ(14)によって汲
上げられた液溜部(2)中の吸収液が供給され、棒状体
(11)に向って噴射される。かかる棒状体(11)か
らなるベンチュリースクラバ(13)は多量の液滴を発
生し、悪臭ガスを通過させると悪臭成分を効率良く吸収
することができる。しかも棒状体(11)の種類や間隙
を変えることによりその特性を自由に変えられる利点を
持つ、しかしベンチュリースクラバ(13)としてはそ
の他の一般的な形式のものを用いても良いことは言うま
でもない。
In the wet cleaning chamber (7), for example, a plurality of rod-shaped bodies (11) having circular, elliptical or polygonal cross sections are arranged in parallel and close to each other, and the gaps between the rod-shaped bodies (11) are used as venturi. A venturi scrubber (13) with a spray nozzle (12) arranged above is provided. The absorption liquid in the liquid reservoir (2) pumped up by the circulation pump (14) is supplied to the spray nozzle (12) and is sprayed toward the rod-shaped body (11). The Venturi scrubber (13) made of such a rod-shaped body (11) generates a large amount of droplets, and when malodorous gas is passed through it, it can efficiently absorb malodorous components. Moreover, it has the advantage that its characteristics can be freely changed by changing the type and gap of the rod-shaped body (11), but it goes without saying that other general types of Venturi scrubbers (13) may also be used. .

一方、乾式吸着室(9)には布状もしくは紙状の吸着材
を断面菊花状の円筒形状に折りたたんだカートリッジ状
の吸着濾材(15)が仕切板(16)から垂下させて設
けられている。この吸着濾材(15)に使用される吸着
材は祇やフェルト等に炭素繊維を付着させたり炭素繊維
布を密着させたりしたものであるが、必ずしもこれに限
定されるものではない。
On the other hand, in the dry adsorption chamber (9), a cartridge-shaped adsorption filter material (15) made by folding a cloth-like or paper-like adsorbent material into a cylindrical shape with a chrysanthemum-like cross section is provided hanging from the partition plate (16). . The adsorbent used for this adsorption filter medium (15) is one made by adhering carbon fibers to wool or felt, or adhering carbon fiber cloth, but is not necessarily limited thereto.

なお、(17)は仕切板(16)の上面に各吸着濾材(
15)に対向させて取付けた逆洗用のペンチエリ−1(
18)は各ペンチエリ−(17)に逆洗用の空気を吹込
むためのノズル管、(19)は清浄ガス吸引用のファン
である。
In addition, (17) is attached to each adsorption filter medium (
15) for backwashing installed opposite to the
18) is a nozzle pipe for blowing air for backwashing into each pentier (17), and (19) is a fan for sucking clean gas.

(作用) このように構成されたものは、入口(6)から悪臭ガス
を送り込めば、悪臭ガスは湿式洗浄室(7)に設けられ
たベンチュリースクラバ(13)の平行に近接配置され
た複数の棒状体(11)の間隙を50〜100g+ 7
秒の高速度で通過するが、この際にその上方のスプレー
ノズル(12)から噴射される吸収液が多量の液滴とな
り、悪臭成分はこれらの液滴に吸収される。ここで発生
した液滴は次にエリミネータ(4)を通過する際に慣性
力によってそのジグザグ状の壁面と衝突して補集され、
下部の液溜部(2)に落下する。またエリミネータ(4
)を通過した微量の悪臭成分を含むガスは乾式吸着室(
9)に導入されるが、このガス中の悪臭成分は吸着濾材
(15)を通過する間に吸着補集される。吸着濾材(1
5)は布状もしくは紙状の吸着材を断面菊花状の円筒形
状に折りたたんだ吸着面積の大きいものであり、しがち
ガスの短絡のおそれのないものであるから悪臭成分を効
率良く吸着除去することができ、通過ガスは清浄ガスと
なって出口(8)から排出される。
(Function) With this structure, if the malodorous gas is sent from the inlet (6), the malodorous gas will be removed from the venturi scrubbers (13) installed in the wet cleaning chamber (7). The gap between the rod-shaped body (11) is 50 to 100g + 7
It passes at a high speed of seconds, and at this time, the absorption liquid sprayed from the spray nozzle (12) above it becomes a large number of droplets, and the malodorous components are absorbed by these droplets. When the droplets generated here next pass through the eliminator (4), they collide with the zigzag wall surface due to inertia and are collected.
It falls into the liquid reservoir (2) at the bottom. Also Eliminator (4
) The gas containing trace amounts of malodorous components is transferred to a dry adsorption chamber (
9), the malodorous components in this gas are adsorbed and collected while passing through the adsorption filter medium (15). Adsorption filter medium (1
5) is a cloth-like or paper-like adsorbent folded into a cylindrical shape with a chrysanthemum-like cross section, which has a large adsorption area, and there is no risk of gas short-circuiting, so it efficiently adsorbs and removes malodorous components. The passing gas becomes clean gas and is discharged from the outlet (8).

なお悪臭ガスがダストを含有する場合には、使用中にダ
ストが吸着濾材(15)の表面に次第に堆積して圧力損
失が増加することとなるので、適当なインターバルで逆
洗用のペンチエリ−(17)にノズル管(18)から空
気を吹込み、ダストを払落とすことができる。
If the malodorous gas contains dust, the dust will gradually accumulate on the surface of the adsorption filter medium (15) during use, increasing the pressure loss. 17) from the nozzle pipe (18) to blow off the dust.

また第2図に示される第2の実施例においては、第1の
実施例の構成に加えて、乾式吸着室(9)の吸着濾材(
15)の下面に浅箱状のプリコート剤収納箱(20)が
設けられ、その内部に活性炭粉末やゼオライト粉末のよ
うな吸着剤粉末(21)が収納されるとともに、その上
面には下向きのノズル(22)が設けられている。この
第2の実施例の装置においては、悪臭ガス成分が濃くな
ったり発生量が多くなり、吸着濾材(15)の吸着能力
が短時間で飽和すると予想されるときには電磁弁(23
)を開いてノズル(22)から吸着剤粉末(21)を吹
き上げ、吸着剤粉末(21)を吸着濾材(15)の表面
にプリコートすることができる。これによって吸着濾材
(15)の耐用期間を延ばすことができ、また逆洗によ
ってプリコートを剥がし、再度プリコートすることも自
由にできるので吸着濾材(15)を交換することなく長
期間にわたり使用することが可能となる。なおプリコー
トされる吸着剤粉末(21)をゼオライト等に交換すれ
ば、活性炭によっては除去できない悪臭成分をも吸着で
きることとなり、多成分ガスにも対応できる。
Furthermore, in the second embodiment shown in FIG. 2, in addition to the structure of the first embodiment, the adsorption filter medium (
15) A shallow box-shaped precoat agent storage box (20) is provided on the bottom surface, and an adsorbent powder (21) such as activated carbon powder or zeolite powder is stored inside the box, and a downward nozzle is provided on the top surface. (22) is provided. In the apparatus of this second embodiment, when the malodorous gas components become concentrated or generated in large quantities and the adsorption capacity of the adsorption filter medium (15) is expected to be saturated in a short time, the solenoid valve (23) is used.
) can be opened to blow up the adsorbent powder (21) from the nozzle (22) and pre-coat the adsorbent powder (21) onto the surface of the adsorption filter medium (15). This makes it possible to extend the service life of the adsorption filter medium (15), and since the precoat can be removed by backwashing and precoated again, the adsorption filter medium (15) can be used for a long period of time without having to be replaced. It becomes possible. If the pre-coated adsorbent powder (21) is replaced with zeolite or the like, malodorous components that cannot be removed by activated carbon can also be adsorbed, making it possible to handle multi-component gases.

(発明の効果) 本発明は以上の説明からも明らかなように、悪臭ガスを
単一の装置で脱臭処理することができるうえ、布状もし
くは紙状の吸着材を断面菊花状の円筒形状に折りたたん
だ吸着濾材を用いることにより、必要以上に多量の吸着
剤を用いることなく確実に悪臭ガス成分の吸着を行わせ
ることができる。よって本発明は従来のこの種のガス清
浄装置の問題点を一掃したものとして、その実用的価値
は極めて大である。
(Effects of the Invention) As is clear from the above description, the present invention is capable of deodorizing foul-smelling gas with a single device, and also converts a cloth-like or paper-like adsorbent into a cylindrical shape with a chrysanthemum-like cross section. By using a folded adsorption filter medium, malodorous gas components can be reliably adsorbed without using an unnecessarily large amount of adsorbent. Therefore, the present invention has extremely great practical value as it eliminates the problems of conventional gas purifying devices of this type.

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

第1図は本発明の第1の実施例を示す断面図、第2図は
第2の実施例を示す断面図である。 (1):ケーシング、(2):液溜部、(4):エリミ
ネータ、(5):隔壁、(7):湿式洗浄室、(9):
乾式吸着室、(13)+ベンチュリースクラバ。
FIG. 1 is a sectional view showing a first embodiment of the present invention, and FIG. 2 is a sectional view showing a second embodiment. (1): Casing, (2): Liquid reservoir, (4): Eliminator, (5): Partition, (7): Wet cleaning chamber, (9):
Dry adsorption chamber, (13) + venturi scrubber.

Claims (1)

【特許請求の範囲】[Claims] 底部を液溜部(2)としたケーシング(1)の内部を、
下部に邪魔板状のエリミネータ(4)を備えた隔壁(5
)によってベンチュリースクラバ(13)を備えた湿式
洗浄室(7)と、布状もしくは紙状の吸着材を断面菊花
状の円筒形状に折りたたんだ吸着濾材(15)を備えた
乾式吸着室(9)とに区画したことを特徴とするガス清
浄装置。
The inside of the casing (1) with the bottom as the liquid reservoir (2),
A bulkhead (5) with a baffle plate-like eliminator (4) at the bottom.
) and a dry adsorption chamber (9) equipped with a wet cleaning chamber (7) equipped with a Venturi scrubber (13) and an adsorption filter material (15) made of cloth or paper-like absorbent material folded into a cylindrical shape with a chrysanthemum cross section. A gas purifying device characterized by being divided into.
JP61253916A 1986-10-23 1986-10-23 GASUSEIJOSOCHI Expired - Lifetime JPH0228373B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61253916A JPH0228373B2 (en) 1986-10-23 1986-10-23 GASUSEIJOSOCHI

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61253916A JPH0228373B2 (en) 1986-10-23 1986-10-23 GASUSEIJOSOCHI

Publications (2)

Publication Number Publication Date
JPS63107727A true JPS63107727A (en) 1988-05-12
JPH0228373B2 JPH0228373B2 (en) 1990-06-22

Family

ID=17257815

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61253916A Expired - Lifetime JPH0228373B2 (en) 1986-10-23 1986-10-23 GASUSEIJOSOCHI

Country Status (1)

Country Link
JP (1) JPH0228373B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001024910A1 (en) * 1999-10-07 2001-04-12 Lab S.A. Method and installation for purifying fumes containing organic pollutants
WO2005032608A1 (en) * 2003-10-02 2005-04-14 Osaka Gas Chemicals Co., Ltd. Gas adsorbing filter
JP2014188512A (en) * 2013-03-28 2014-10-06 Metawater Co Ltd Deodorization apparatus

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104307345B (en) * 2014-11-19 2016-05-04 广西南宁华国环境科技有限公司 A kind of coal smoke desulfurization and dust removal device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001024910A1 (en) * 1999-10-07 2001-04-12 Lab S.A. Method and installation for purifying fumes containing organic pollutants
FR2799388A1 (en) * 1999-10-07 2001-04-13 Lab Sa METHOD AND SYSTEM FOR PURIFYING SMOKE CONTAINING ORGANIC POLLUTANTS
WO2005032608A1 (en) * 2003-10-02 2005-04-14 Osaka Gas Chemicals Co., Ltd. Gas adsorbing filter
JP2014188512A (en) * 2013-03-28 2014-10-06 Metawater Co Ltd Deodorization apparatus

Also Published As

Publication number Publication date
JPH0228373B2 (en) 1990-06-22

Similar Documents

Publication Publication Date Title
US8241398B2 (en) Method and apparatus for the enhanced removal of aerosols and vapor phase contaminants from a gas stream
JP2008520333A (en) Wet air purifier
JP2015073990A (en) Method and apparatus for wet desulfurization spray towers
KR102068067B1 (en) Exhaust System for Painting Booth
US7077740B2 (en) Paint spray booth
KR101595218B1 (en) Gas purification apparatus
US4548623A (en) Perforated trough conditioning device
JPS63107727A (en) Gas cleaning apparatus
KR101321602B1 (en) Wet Typer of Apparatus for Filtering with Function of Cleaning, Air Freshener,Sterilization and Humidification
KR200309268Y1 (en) An air purifier by waterwashing
KR100328676B1 (en) Exhaust gas treatment apparatus of tenter
JP2006175336A (en) Wet gas purifier
JP3870375B2 (en) Air purification device
KR20210051954A (en) Multi complex dust collecting device
JPS62163721A (en) Gas purifier
JPH0160290B2 (en)
JP2002000709A (en) Air cleaner
JP7418045B2 (en) Deodorizing equipment and method
GB2246525A (en) Gas-cleaning apparatus
KR102281763B1 (en) Harmful gas reduction device
CN215661221U (en) Novel environmental protection type banbury mixer that removes dust
JP3017276U (en) Air purifier
KR102646807B1 (en) No filter media purifier scrubber
JPH043617Y2 (en)
RU2318579C1 (en) Device for purifying and wetting of the gases