JPS60212205A - Wet dust removing apparatus - Google Patents

Wet dust removing apparatus

Info

Publication number
JPS60212205A
JPS60212205A JP6871584A JP6871584A JPS60212205A JP S60212205 A JPS60212205 A JP S60212205A JP 6871584 A JP6871584 A JP 6871584A JP 6871584 A JP6871584 A JP 6871584A JP S60212205 A JPS60212205 A JP S60212205A
Authority
JP
Japan
Prior art keywords
water
dust
tank
air
dust collection
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
JP6871584A
Other languages
Japanese (ja)
Inventor
Tsuchio Nagata
永田 鎚雄
Megumi Hosoda
細田 恵
Masayoshi Ayukawa
鮎川 正義
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.)
KUKEN KIKO KK
Original Assignee
KUKEN KIKO 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 KUKEN KIKO KK filed Critical KUKEN KIKO KK
Priority to JP6871584A priority Critical patent/JPS60212205A/en
Publication of JPS60212205A publication Critical patent/JPS60212205A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To contrive to reduce operation cost, in a wet dust collection apparatus, by providing a water sprinkling dust collection tower for separating dust from air, water tanks used in sprinkling and recirculating water and a sewage separator for separating dust from water by centrifugal separation. CONSTITUTION:A dust-containing air stream air stream enters from an air intake port 1 and the dust in the air stream is collected by washing water, which is supplied from a water distributor 5 and scattered by a rotating metal net rotor 4, and collected in the water tank 3 under a dust collection tower as dust water while air is exhausted from an exhaust port 22. The dust water enters a sewage separator and centrifugally separated into dust and water by a rotary basket 10 while water is discharged to the water tank 13 from a water receiving tank 11 by a fall and positively foamed to adsorb fine dust by foam. The foam enters a dust accumulation chamber 25 through a chute 19 and washing water is supplied to the water distributor through a water feed pipe 15 by a recirculation pump 14.

Description

【発明の詳細な説明】 この発明は空気中の粉塵を除去する装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for removing dust from the air.

穀物処理場等で多歌に発生する籾殻等の粉塵処理に関し
ては、従来サイクロン、バッグフィルター等による乾式
処理による方法と、湿式処理による方法に大別される。
Regarding the treatment of dust such as rice husks generated in grain processing plants, etc., there are two main methods: dry treatment using conventional cyclones, bag filters, etc., and wet treatment.

湿式処理の場合、穀物粉塵が有する難混性、浮遊性、又
は粗度の条件にはばまれ、−室を設けて風の速度を緩和
し、粗大塵を塵室に沈降させ、−次沈降処理をした含塵
空気を塵室から湿式処理室に導き、洗浄水によって濾過
する乾・湿二元処理が普及している。一般に普及してい
る方式は向流スクラバ一方式で、設備に押込まれ、そこ
で水滴微細化して除塵効果を上げようとすれば、微細な
水滴が気流に乗り、外部に排気され、二次公害を招く結
果となっている。
In the case of wet processing, grain dust is difficult to mix, buoyant, or coarse, so a chamber is installed to reduce the wind speed, allowing the coarse dust to settle in the dust chamber, and then settling. Two-way dry/wet treatment is becoming popular, in which treated dust-containing air is guided from a dust chamber to a wet treatment chamber and filtered using washing water. The generally popular method is a single-type countercurrent scrubber, in which water is forced into equipment, where water droplets are made finer to improve the dust removal effect.The fine water droplets ride on the airflow and are exhausted to the outside, causing secondary pollution. This has resulted in an invitation.

エリミネータ−等を設けて排出空気の水滴を分離する構
造としているが、固定式のため目詰りをおこし、風圧の
損失が大きくなる結果となり不十分であった。
Although an eliminator or the like is installed to separate water droplets from the discharged air, the fixed type causes clogging and results in a large loss of wind pressure, which is insufficient.

又、洗浄水は反復使用する方式が一般的であるが大きな
水槽を必要としている。従来体系の問題点として、塵室
に沈降した乾いた粉塵の搬出、搬送の除去作業時に再飛
散を生じ、二次公害の要因となる例が多い。又、大量の
洗浄水が必要であることから水槽が大型となり、沈澱す
る汚泥の除去のため、補器類が必要なため装置全体が大
きくなり大容量のポンプが必要で所要動力が大きくなる
In addition, although washing water is generally used repeatedly, it requires a large water tank. A problem with the conventional system is that the dry dust that has settled in the dust chamber is often re-dispersed during removal and transport operations, causing secondary pollution. Furthermore, since a large amount of washing water is required, the water tank becomes large, and auxiliary equipment is required to remove the settled sludge, making the entire device large and requiring a large-capacity pump, which increases the power required.

又、大量の懸濁した汚水の処理、悪臭で困る場合がある
In addition, there may be problems with the treatment of large amounts of suspended sewage and bad odors.

これらの欠点を除くため本発明は (1) 乾式処理部(−次沈降室)をなくし、一括湿式
処理とし、粉塵の再飛散を防止する。
In order to eliminate these drawbacks, the present invention (1) eliminates the dry processing section (secondary settling chamber) and performs a batch wet processing to prevent dust from scattering again.

(2) 粉塵除去装置は圧力損失か少く、施設からの排
出される排気エネルギーを有効に利用し補助送風機を必
要としない。
(2) The dust removal device has little pressure loss, effectively utilizes the exhaust energy exhausted from the facility, and does not require an auxiliary blower.

(3) 粉塵の性状に応じて処理できるコンノシクトな
装置とし、立体配置も可能で地上スペースを少くする。
(3) It is a consummate device that can process dust according to its properties, and can be arranged in three dimensions to reduce the amount of space on the ground.

(4) 洗浄水は循環により反復使用するが、水槽を小
型にし、循環水を少くし、補給水による希釈効果を高め
、攪拌式の水槽で汚泥の沈澱をなくする。
(4) Washing water is recycled and used repeatedly, but the water tank is made smaller, the amount of circulating water is reduced, the dilution effect of make-up water is increased, and the agitation type water tank is used to eliminate sludge sedimentation.

(2)(4)により処理に要する動力を少くし、運転経
費の減少をはかることを目的としたもので、図について
説明すれば第1図は集塵塔で一種のサイクロンスクラバ
ーであって円筒接続に空気取入口(1)をもった外筒(
2)と速度成分をもった含塵気流で自転する金網ロータ
ー(4)、下部水槽(3)、排気口(イ)で構成されて
いる。その作用は円筒接続方向より押込まれた含塵空気
は円筒内周mGこ沿って旋回気流となるが、含塵空気は
外周に向う遠心気流と中心方向に向う内向気流とに複雑
に分布する。
(2) The aim is to reduce the power required for processing and reduce operating costs through (4). To explain the diagram, Figure 1 shows a dust collection tower, which is a type of cyclone scrubber and has a cylindrical shape. Outer cylinder with air intake (1) at the connection (
2), a wire mesh rotor (4) that rotates on its own axis using a dust-containing airflow with a velocity component, a lower water tank (3), and an exhaust port (a). The effect is that the dust-containing air pushed in from the cylinder connection direction becomes a swirling airflow along the inner circumference mG of the cylinder, but the dust-containing air is complicatedly distributed into a centrifugal airflow toward the outer circumference and an inward airflow toward the center.

この部分に含塵気流の速度成分に押され自転する金網ロ
ーター(4)を置き、更にその上部の分水器(5)から
洗浄水を流下させる。洗浄水は金網ローターの回転によ
って飛散水となり、旋回気流の影響で水滴の気体に対す
る相対移動距離か長くなり、且つ、気体と水滴の運動方
向は直交流や並流となって気液接触は増大する。水滴と
接触して質量を増した粉塵は沈降点に達して落下ないし
遠心気流に沿って円周壁の液膜に接触して捕集され、原
水となって集塵塔下部水槽(3)に捕集される。筒内で
内向気流となった空気は自転する金網ローターの漏れ表
面に接触して更に濾過され金網ローター内面に沿って強
制渦を形成し、排気筒床面■)に衝突する。この時空気
は洗浄水、細粉塵を残して排気口に)より放出する。尚
、排気筒床面(イ)には液膜状に洗浄水が流れているの
でさらに捕集効果がある金網ローターに付着しようとす
る粉塵は洗浄水が上方および側面より流れているが、ロ
ーターの回転によって金網面を洗いながら外周方向に振
り切られるため、金網の目詰りによる機能低下はない第
2図は汚水分離機でその構成は下部水槽から送り込まれ
た含塵水を、座体と水とに連続的に分離する回転式バス
ケy ) (10)とこのノくスケ7)を通過した洗浄
水を受ける水受タンク(ロ)、ノくスケ、ト上から連続
的に排出する座体の飛散を防止する分離機外筒(9)よ
りなる。作用は遠心脱水方式であるため排出する座体は
堅絞りで粉塵集積室(イ)に降積するため、除去Φ搬出
における粉塵の二次曲数はない。含塵水に含まれている
細粉塵は瞬時Gこ脱水するため、粗粉塵が11aiとな
って除去される。
A wire mesh rotor (4) that rotates due to the velocity component of the dust-containing airflow is placed in this area, and washing water is made to flow down from a water separator (5) above the rotor. The cleaning water becomes scattered water due to the rotation of the wire mesh rotor, and the relative movement distance of the water droplets to the gas becomes longer due to the influence of the swirling air current, and the direction of movement of the gas and water droplets becomes cross flow or parallel flow, increasing gas-liquid contact. do. The dust, which increases in mass when it comes into contact with water droplets, reaches the settling point and falls or is collected by contacting the liquid film on the circumferential wall along the centrifugal air current, becoming raw water and being collected in the water tank (3) at the bottom of the dust collection tower. collected. The air that has become an inward flow inside the cylinder comes into contact with the leaking surface of the rotating wire mesh rotor, is further filtered, forms a forced vortex along the inner surface of the wire mesh rotor, and collides with the exhaust pipe floor surface (2). At this time, the air is released through the exhaust port, leaving behind the cleaning water and fine dust. Furthermore, since the cleaning water flows in the form of a liquid film on the exhaust pipe floor surface (A), the dust that tries to adhere to the wire mesh rotor, which has a further collection effect, is removed by the cleaning water flowing from above and from the side. Figure 2 shows a sewage separator, and its configuration is such that the dust-containing water sent from the lower water tank is transferred to the seat body and the water separator. A rotary basket that is continuously separated into (10) and a water receiving tank (b) that receives the washing water that has passed through the nozzle 7), and a seat body that continuously discharges the water from above the nookuseke and g. It consists of a separator outer cylinder (9) that prevents the particles from scattering. Since the action is a centrifugal dehydration method, the seat body to be discharged is tightly squeezed and deposited in the dust collection chamber (a), so there is no quadratic number of dust during removal Φ transport. Since the fine dust contained in the dust-containing water is dehydrated instantaneously, the coarse dust becomes 11ai and is removed.

第4図は水槽(ロ)で、汚水分離機から排出する洗浄水
は槽内排出に方向性を持たせ、落差によって槽内空間に
放出させ、積極的に発泡させて槽内に懸濁する微粒塵を
泡表面)こ吸着させる。発泡が発達すると槽内空間から
シーートに)を通って粉塵集積室に入る。槽内の洗浄水
は循環ポンプ(ロ)により送水管(ロ)を通り集塵塔上
部の分水器(5)に供給されるが、一部をバイパス管(
ト)の途中に配設された調節弁(ロ)の調節により水槽
(ロ)に還流させ、汚泥沈澱の防止と発泡促進を行って
いる。
Figure 4 shows the water tank (b), where the washing water discharged from the sewage separator is directed into the tank, discharged into the tank space by the head, and actively foamed and suspended in the tank. Allows fine dust to be adsorbed to the foam surface. When the foam develops, it passes through the tank space (through the sheet) and enters the dust collection chamber. The cleaning water in the tank is supplied by the circulation pump (b) through the water pipe (b) to the water divider (5) at the top of the dust collection tower, but some of it is passed through the bypass pipe (b).
The sludge is returned to the water tank (b) by adjusting the control valve (b) located in the middle of g), thereby preventing sludge sedimentation and promoting foaming.

本装置の効果として (1) 乾式処理部(集塵庫)の必要なく粉塵の性状に
応じて処理できるコンパクトな装置C立体配置も可能で
、地上スペースが少くてすむ(2) 集塵塔は圧力損失
が少く機械各部・\の影響も少くサイクロンスクラバー
でランキング渦により粉塵の水滴接触はクロスフローと
なって気液接触効果が高い。
The advantages of this device are (1) A compact device C that can process according to the properties of dust without the need for a dry processing section (dust collection chamber), and can be arranged in three dimensions, requiring less ground space. (2) The dust collection tower There is little pressure loss, and there is little influence from each part of the machine.In the cyclone scrubber, the ranking vortex causes water droplet contact with dust to become a cross flow, resulting in a high gas-liquid contact effect.

(3) 集塵塔内部に自転する金網ローターのフィルタ
ー効果によって複合的に処理される。
(3) The dust is processed in a complex manner by the filter effect of the rotating wire mesh rotor inside the dust collection tower.

放出する排気は金網ローター及び排気筒て直交し、衝突
するため水滴の飛沫同伴がない。
The emitted exhaust gas crosses the wire mesh rotor and the exhaust pipe at right angles and collides with each other, so there is no entrainment of water droplets.

(4)キ原水は連続してセパレーターにより固液外H,
(堅絞り状)して全量を1ケ所に集積するため、除去・
搬出における二次飛散がなく衛生的に作業できる。
(4) The raw water is continuously passed through a separator to provide solid-liquid and external H,
(hard drawing shape) and accumulates the entire amount in one place, removing and
Work can be done hygienically without secondary scattering during transport.

(5)洗浄水は循環により反復使用するが、小量の水で
あるため補給水による希釈効果が大きく、攪拌式の水槽
で汚泥等の沈澱はない。
(5) Washing water is used repeatedly by circulation, but since it is a small amount of water, the dilution effect with make-up water is large, and there is no sedimentation of sludge etc. in the agitating water tank.

(6) 洗浄水は流水飛沫式でノズルを使用せず、メン
テナンスが(0341である。
(6) Cleaning water is a running water splash type, no nozzle is used, and maintenance is (0341).

(7) 耐蝕性に優れた材質を使用し、構造も簡単で、
保守管理も容易で長年の使用に耐える。
(7) Uses materials with excellent corrosion resistance and has a simple structure.
It is easy to maintain and manage and can withstand many years of use.

(8) 処理に要する動力が少く運転経費か安価である
等の利点多し。
(8) It has many advantages such as less power required for treatment and lower operating costs.

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

図面は本発明の一実施態様を示すもので、第1図は集塵
塔斜視図。 第2図は汚水分離様斜視図。 第6図は全体機構図。を示し、 第4図は水槽機構の平面図。 (1)空気取入口 (2)円筒内壁 (3)下部水槽 
(4)金網ローター (5)分水器(6)散水槽 (7
)吐出口 (8)送水管 (9)分離機外筒 (10)
回転バスケット (ロ)水受タンク (ロ)流水管 (
ロ)水槽 (ロ)循環ポンプ に)送水管 (ト)バイ
パス管 αつ調節弁 (ト)案内板 (イ)シ、−ト 
(イ)溢水器 に)給水器 (イ)排気口 に)床面(
ホ)排水管 (ホ)粉塵集積室 A:含塵空気 B:清浄空気 特許出願人 空研機工株式会社 特許出願人 永 1)鎚 雄
The drawings show one embodiment of the present invention, and FIG. 1 is a perspective view of a dust collection tower. FIG. 2 is a perspective view of sewage separation. Figure 6 is a diagram of the overall mechanism. FIG. 4 is a plan view of the aquarium mechanism. (1) Air intake (2) Cylindrical inner wall (3) Lower water tank
(4) Wire mesh rotor (5) Water divider (6) Water tank (7
) Discharge port (8) Water pipe (9) Separator outer cylinder (10)
Rotating basket (b) Water tank (b) Water pipe (
B) Water tank (B) Circulation pump To) Water pipe (G) Bypass pipe α control valve (G) Guide plate (B) C, -T
(a) Water supply device (a) Exhaust port) Floor surface (
E) Drain pipe (E) Dust collection room A: Dust-containing air B: Clean air Patent applicant Kuken Kiko Co., Ltd. Patent applicant Ei 1) Yu Tsuchi

Claims (1)

【特許請求の範囲】 (イ) 粉塵と空気を分離する装置として外筒(2)の
内側に回転する金網ローター(4)を配設し、上部の分
水器(5)より散水する集塵塔。 (ロ)水槽い)として濾過水を受け、水槽底部に取りつ
けられたポンプに)により集塵塔上部より散水用として
使用し、一部水槽内に循環水として使用される水槽。 (ハ)分離装置として外筒(9)の内側に回転する断面
V字形の回転式バスケy ) (10)を配設し、遠心
脱水方式により粉塵と水を分離する汚水分離機。 堤上の如く(イ)(ロ)(ハ)より構成された湿式除塵
装置
[Claims] (a) A dust collection device in which a rotating wire mesh rotor (4) is disposed inside the outer cylinder (2) as a device for separating dust and air, and water is sprinkled from an upper water divider (5). Tower. (b) A water tank that receives filtered water as a water tank, is used for watering from the top of the dust collection tower by a pump attached to the bottom of the tank, and is used partly as circulating water within the tank. (c) A sewage separator that separates dust and water using a centrifugal dehydration method, in which a rotating basket (10) with a V-shaped cross section is disposed inside an outer cylinder (9) as a separating device. A wet dust removal device consisting of (a), (b), and (c)
JP6871584A 1984-04-05 1984-04-05 Wet dust removing apparatus Pending JPS60212205A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6871584A JPS60212205A (en) 1984-04-05 1984-04-05 Wet dust removing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6871584A JPS60212205A (en) 1984-04-05 1984-04-05 Wet dust removing apparatus

Publications (1)

Publication Number Publication Date
JPS60212205A true JPS60212205A (en) 1985-10-24

Family

ID=13381760

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6871584A Pending JPS60212205A (en) 1984-04-05 1984-04-05 Wet dust removing apparatus

Country Status (1)

Country Link
JP (1) JPS60212205A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104258670A (en) * 2014-07-31 2015-01-07 安徽光明槐祥工贸集团有限公司 Rice hull ash collection method by spraying
CN106039903A (en) * 2016-07-13 2016-10-26 方龙旺 Centrifugal dust filtering device
CN106555232A (en) * 2016-12-07 2017-04-05 广西凯喜雅丝绸有限公司 The water jet of battage bath
CN111020220A (en) * 2019-12-09 2020-04-17 李素侠 Refining device of secondary aluminum
CN111491739A (en) * 2017-12-19 2020-08-04 巴工业株式会社 Disc type centrifugal separator
WO2022131316A1 (en) * 2020-12-18 2022-06-23 株式会社上野商店 Air purifier

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104258670A (en) * 2014-07-31 2015-01-07 安徽光明槐祥工贸集团有限公司 Rice hull ash collection method by spraying
CN106039903A (en) * 2016-07-13 2016-10-26 方龙旺 Centrifugal dust filtering device
CN106039903B (en) * 2016-07-13 2018-06-19 江苏赛维环保有限公司 A kind of centrifugal dust filtration device
CN106555232A (en) * 2016-12-07 2017-04-05 广西凯喜雅丝绸有限公司 The water jet of battage bath
CN111491739A (en) * 2017-12-19 2020-08-04 巴工业株式会社 Disc type centrifugal separator
CN111491739B (en) * 2017-12-19 2022-06-03 巴工业株式会社 Disc type centrifugal separator
CN111020220A (en) * 2019-12-09 2020-04-17 李素侠 Refining device of secondary aluminum
CN111020220B (en) * 2019-12-09 2021-11-12 湖南同和新材料有限公司 Refining device of secondary aluminum
WO2022131316A1 (en) * 2020-12-18 2022-06-23 株式会社上野商店 Air purifier

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