JPS6269033A - Dust and germ removing device for gas - Google Patents

Dust and germ removing device for gas

Info

Publication number
JPS6269033A
JPS6269033A JP60207584A JP20758485A JPS6269033A JP S6269033 A JPS6269033 A JP S6269033A JP 60207584 A JP60207584 A JP 60207584A JP 20758485 A JP20758485 A JP 20758485A JP S6269033 A JPS6269033 A JP S6269033A
Authority
JP
Japan
Prior art keywords
water
tower
ozone
removal
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.)
Granted
Application number
JP60207584A
Other languages
Japanese (ja)
Other versions
JPH0325702B2 (en
Inventor
Kiyokatsu Ueda
上田 清勝
Akira Ishikawa
彰 石川
Takeo Takahashi
高橋 武男
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP60207584A priority Critical patent/JPS6269033A/en
Publication of JPS6269033A publication Critical patent/JPS6269033A/en
Publication of JPH0325702B2 publication Critical patent/JPH0325702B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/10Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
    • F24F8/117Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using wet filtering
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/10Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
    • F24F8/117Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using wet filtering
    • F24F8/133Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using wet filtering by direct contact with liquid, e.g. with sprayed liquid
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/10Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
    • F24F8/117Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using wet filtering
    • F24F8/142Treatment of used liquid, e.g. cleaning for recycling
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/20Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation
    • F24F8/24Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation using sterilising media
    • F24F8/26Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation using sterilising media using ozone
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Central Air Conditioning (AREA)

Abstract

PURPOSE:To make small the size of a device to remove dust and germs in gas and raise its efficiency by providing a cleaning water circulating and supplying system with a spray nozzle and ozone supplying means to supply ozone for sterilization of the water in the pool at the bottom section of a water tower, and water drop removal means and ozone removal device installed on the gas exhaust side of a water cleaning tower. CONSTITUTION:In a cleaning water circulating and supplying system installed to a water cleaning tower 5, a water atomization spray nozzles to be installed in the tower are provided in upper stage spray nozzle group 7a and lower stage spray nozzle group 7b. The water cleaning tower 5 in provided with, an ozonizer 14 which generates ozone as a sterilizer and an ozone supply means which draws ozone from the ozonizer 14 and consists of an ozone supply nozzle 15 as a bubble-generating device provided at the liquid pool of the bottom section of the water cleaning tower 5. Further, in addition an eliminator 16 for removal of water drops is provided as water drop removal means on the exhaust side of the water cleaning tower 5, and at the rear stage of the water cleaning tower 5 a water drop removal cyclone 17 for removal of water drops and an active charcoal filter 18 which removes ozone from the gas are provided. In the drain water discharge pipe route, a filtering device for the discharged cleaning water is inserted.

Description

【発明の詳細な説明】[Detailed description of the invention] 【発明の属する技術分野】[Technical field to which the invention pertains]

この発明は食品加工室5食品保管室、病院における手術
室、病室、その他の無菌作業所等を対象に室内空気の除
塵、除菌を行って清浄化するようにした気体の除塵・除
菌装置に関する。
This invention is a gaseous dust removal and sterilization device that cleans indoor air by removing dust and sterilization from food processing rooms, food storage rooms, operating rooms in hospitals, hospital rooms, and other sterile workplaces. Regarding.

【従来技術とその問題点】[Prior art and its problems]

まず第2図により頭記した気体の除塵・除菌装置の従来
における一般的なシステムを説明する。 図において、1は空気清浄化の対象となる食品加工室等
の室であり、謹呈lの空気取出口と給気口との間に空気
循環送風路2を構成し、ここに送風機33粗大な塵埃を
除去するプレフィルタ4.水洗塔5.および空!1M装
置6が順に介装設置され、これらで除塵・除菌装置のシ
ステムを構成している。ここで前記の水洗塔5は塔内に
微少水滴を噴霧するスプレーノズル7、送水ポンプ8.
水濾過器9等の間を結んで成る水噴霧系を装備した噴霧
式洗浄集塵器として構成されている。 かかる構成で送風機3により室1より引き出された塵埃
、菌を含む室内の汚染空気は、まずプレフィルタ4で粗
大な塵埃を取り除いた後に水洗塔5の塔内下部へ導入さ
れる。ここで汚染空気は塔内を矢印Aのように上昇する
過程でスプレーノズル7から噴霧して塔内空間に充満す
る微細な水滴粒子Bと接触し、空気中に含まれている微
粒子塵埃および塵埃に付着ている菌等は洗浄集塵作用に
より水滴へ移行して空気流から分離補集され、塔内を沈
降して底部に溜る。一方、除塵、除菌して清浄化された
空気流は塔上部から排出され、さらに空!PJ装置6で
温度、湿度を調整した後に再び室1内に送気還流される
。一方、水洗塔5内の底部に溜った水は活性炭、イオン
交換樹脂等の吸着物質を内蔵した濾過器9で濾過した後
に、送水ポンプ8を経て再びスプレーノズル7から塔内
に噴霧されるように循環して反復使用される。なおlO
は定期的に塔内の洗浄水を交換する際に洗浄廃水を系外
に排水するドレン弁である。 ところで上記した従来の除塵・除菌装置の構成には次記
のような問題点がある。すなわち、まず水洗塔5での除
塵、除菌効率を上げるには、塔内を下方から上方へ向け
て通流する空気流Aとスプレーノズル7から塔内に分散
噴霧する水滴粒子Bとの接触割合および衝突の相対速度
を高めて塵埃。 菌の補集率を高める必要がある。このためにはスプレー
ノズル7の噴霧口を小さく、かつ噴射速度を高めて微細
な水滴粒子を数多く発生し、これにより同じ水量での水
滴表面積を増大させて空気流との接触割合の増加を図る
方法が一般に採られているが、スプレーノズルから噴霧
する水滴粒子径が微少になる程塔内を上昇する空気流の
影響を受は易くなり、水滴粒子は塵埃、菌を取り込んだ
まま塔内を上昇する空気流に運ばれて水洗塔5から外方
へ逸出する割合が多くなり、このままでは除塵、除菌効
率が低下する。一方、このような水滴粒子の塔外逸出を
避けるためには塔内の流れる空気流の風速を下げる手段
も考えられるが、このために同じ空気量を処理するの番
ご水洗塔5が径大となり設備が大形化する問題が派生す
る。 また別な問題として上記した従来装置では、水洗塔5内
で汚染空気流中に含まれている菌、ないし空気流から洗
浄集塵して分離補集した菌に対してはこれを積極的に滅
菌する手段を備えてなく、このままでは水洗塔内での水
噴霧により補集し切れなかった空気流中の菌が生存した
まま空気流に乗って水洗塔5から下流側へ逸出する他、
水洗塔内で補集された苗が液溜りに滞留している水中で
繁殖し、噴霧シャr′−の菌に、よる汚染度が増大する
問題が残る。この場合に洗浄水を頻繁に系外へ排出し、
この排水を消毒滅菌した上で排水処理することも考えら
れるが、大容量の水洗塔では噴霧に使用する洗浄水量も
多く、その都度洗浄水を廃棄処分することは洗浄水の消
費量が増して運転コストが増大する。
First, a conventional general system of the gaseous dust removal and sterilization device described above with reference to FIG. 2 will be explained. In the figure, 1 is a room such as a food processing room that is the target of air purification, and an air circulation and blowing passage 2 is constructed between the air intake port and the air supply port of the room 1. Pre-filter to remove dust 4. Washing tower 5. and sky! The 1M devices 6 are installed in order, and these devices constitute a dust removal and sterilization device system. Here, the water washing tower 5 includes a spray nozzle 7 that sprays minute water droplets into the tower, a water pump 8.
It is constructed as a spray type cleaning dust collector equipped with a water spray system that connects water filters 9 and the like. With this configuration, the indoor contaminated air containing dust and bacteria drawn out from the room 1 by the blower 3 is introduced into the lower part of the washing tower 5 after first removing coarse dust with the pre-filter 4. Here, while the contaminated air rises inside the tower as shown by arrow A, it comes into contact with fine water droplets B that are sprayed from the spray nozzle 7 and fills the space inside the tower, and the particulate dust and dirt contained in the air are removed. Bacteria and the like adhering to the tower are transferred to water droplets by the cleaning and dust collection action, separated and collected from the air flow, and then settle in the tower and accumulate at the bottom. On the other hand, the air stream that has been purified through dust removal and sterilization is discharged from the top of the tower, and is even emptier! After adjusting the temperature and humidity with the PJ device 6, the air is sent back into the room 1 again. On the other hand, the water accumulated at the bottom of the water washing tower 5 is filtered by a filter 9 containing adsorbent substances such as activated carbon and ion exchange resin, and then passed through the water pump 8 and sprayed into the tower from the spray nozzle 7 again. used repeatedly. Furthermore, lO
is a drain valve that drains cleaning waste water out of the system when the cleaning water in the tower is replaced periodically. However, the configuration of the conventional dust removal/sterilization device described above has the following problems. That is, first of all, in order to increase the dust removal and sterilization efficiency in the water washing tower 5, the air flow A flowing from the bottom to the top inside the tower comes into contact with the water droplet particles B dispersed and sprayed into the tower from the spray nozzle 7. Dust increasing the proportion and relative speed of collision. It is necessary to increase the bacterial collection rate. For this purpose, the spray nozzle 7 is made smaller and the spray speed is increased to generate many fine water droplets, thereby increasing the surface area of the water droplets with the same amount of water and increasing the contact ratio with the air flow. This method is generally adopted, but the smaller the size of the water droplets sprayed from the spray nozzle, the more susceptible they are to the influence of the airflow rising inside the tower, and the water droplets continue to move inside the tower while taking in dust and bacteria. A large proportion of the air is carried away by the rising airflow and escapes from the washing tower 5 to the outside, and if this continues, the efficiency of dust removal and sterilization will decrease. On the other hand, in order to prevent such water droplets from escaping outside the tower, it is possible to reduce the wind speed of the air flowing inside the tower. This results in the problem of larger equipment. Another problem is that with the above-mentioned conventional device, bacteria contained in the contaminated air stream in the water washing tower 5 or bacteria separated and collected by washing and collecting dust from the air stream are actively removed. There is no means for sterilization, and as it stands, bacteria in the air stream that could not be collected by the water spray inside the washing tower will remain alive and escape from the washing tower 5 downstream from the washing tower 5 while remaining alive.
The problem remains that the seedlings collected in the water washing tower multiply in the water stagnant in the water pool, increasing the degree of contamination by bacteria in the spray tank. In this case, frequently drain the wash water out of the system.
It is possible to treat this wastewater after disinfecting and sterilizing it, but large-capacity washing towers use a large amount of washing water for spraying, and disposing of washing water each time would increase the amount of washing water consumed. Operating costs increase.

【発明の目的】[Purpose of the invention]

この発明番よ上記の点にかんがみなされたものであり、
前記した従来装置の欠点を除去して小型な構成でかつ除
塵、除菌効率が高く、併せて菌の滅菌処理が行えるよう
にした気体の清浄化に対する綜合的な性能、信頼性の高
い除塵・除菌装置を提供することを目的とする。
This invention number was taken into consideration in view of the above points,
Eliminating the drawbacks of the conventional device described above, the device has a compact structure, has high dust removal and sterilization efficiency, and has comprehensive performance for gas purification and highly reliable dust removal and sterilization. The purpose is to provide a sterilization device.

【発明の要点】[Key points of the invention]

上記目的を達成するために、この発明は水洗塔内に上下
段に分割配備されてその下段側からは微細水滴粒子、上
段側からは粗大水滴粒子のシャワーを汚染気体に向けて
噴霧するスプレーノズルを含む洗浄水の循環供給系と、
塔内底部の液溜りの水中に殺菌剤としてのオゾンを供給
するオゾン供給手段と、水洗塔の排気側に設置した水滴
除手段およびオゾン除去手段とを具備して構成したもの
である。 かかる構成により、まず水洗塔内の下部領域では微細な
水滴粒子と塔内に導入された汚染気体流との充分な接触
で水滴粒子による汚染気体流中の塵埃粒子、菌の補集効
率を高めつつ、塔内の上部il域では下方から上昇通流
する気体流と一諸に浮上してくる微細水滴粒子を粗大な
水滴粒子により捕捉して下方へ重力沈降させるとともに
、さらに噴霧シャワーの間隙を縫って空気流と一緒に塔
内から下流側へ流出しようとする微細水滴粒子を除滴手
段により空気流から確実に除去することができ、より一
層高い除塵、除菌効率が得られるようになる。さらに加
えて塔内底部の水中にオゾンを供給することにより、洗
浄水中に補集された菌の滅菌処理と並行して水中から塔
内に放散したオゾンガスで汚染空気流中の菌を直接殺菌
処理することができ、かくして綜合的な除塵1除菌性能
の向上が図れるようになる。
In order to achieve the above object, the present invention provides a spray nozzle that is divided into upper and lower stages in a water washing tower, and sprays a shower of fine water droplets from the lower stage and coarse water droplets from the upper stage toward contaminated gas. a cleaning water circulation supply system including;
The tower is equipped with an ozone supply means for supplying ozone as a disinfectant into the water in the liquid pool at the bottom of the tower, and a water droplet removal means and an ozone removal means installed on the exhaust side of the washing tower. With this configuration, firstly, in the lower region of the water washing tower, there is sufficient contact between fine water droplets and the contaminated gas flow introduced into the tower, increasing the efficiency of scavenging dust particles and bacteria in the contaminated gas flow by the water droplets. At the same time, in the upper IL region of the tower, the fine water droplets that come to the surface together with the gas flow flowing upward from below are captured by coarse water droplets and allowed to settle downward by gravity. The fine water droplets that tend to flow out from the tower to the downstream side along with the air flow can be reliably removed from the air flow by the drip removal means, resulting in even higher dust removal and sterilization efficiency. . In addition, by supplying ozone into the water at the bottom of the tower, in parallel with the sterilization of bacteria collected in the cleaning water, the ozone gas released from the water into the tower directly sterilizes bacteria in the contaminated air stream. In this way, comprehensive dust removal and sterilization performance can be improved.

【発明の実施例】[Embodiments of the invention]

第1図はこの発明の実施例を示すものであり、第2図に
対応する同一部材には同じ符号が付しである。すなわち
この発明により、水洗塔5に配備した洗浄水の循環供給
系に付いて、その塔内設置の水噴霧用スプレーノズルが
上下段のスプレーノズル群7aと7bとに分けて配備さ
れている。ここで下段側のスプレーノズル群7bは噴霧
口を小径にして200μI前後の微細水滴粒子シャワー
を噴霧するようなノズルであるのに対し、上段側のスプ
レーノズル群7aは500μ削前後の粗大水滴粒子シャ
ワーを発生するように設定されたノズルとして成る。な
お11は各段のスプレーノズル群への分岐配管に介挿さ
れた流量制御弁、12は塔内へ洗浄水を補給する上水道
の配管、13は同配管に介挿した塔内水位の調節弁であ
る。また水洗塔5には、殺菌剤としてのオゾンを発生さ
せるオゾナイザ14、およびオゾナイザ14から引き出
して水洗塔5の底部液溜りに配備した気泡発生器として
のオゾン供給ノズル15からなるオゾン供給手段が装備
されている。さらに加えて水洗塔5の排気側には除滴手
段として水洗塔5の塔内上部に水滴除去用のエリミネー
タ16が、また水洗塔5の後段に水滴除去用の除滴サイ
クロン17、および気体からオゾンを除去する活性炭フ
ィルタ18が設置されている。なお19はドレン排水管
路に介挿された洗浄排水の濾過器である。 次に上記構成の動作に付いて説明する。運転時にはオゾ
ナイザ14で生成されたオゾンがオゾン供給ノズル15
よりオゾン気泡Cとなって洗浄塔5の塔内底部に溜って
いる洗浄水中に吐出供給され、その一部は水中に溶解し
残りは気泡のまま水中を上昇して塔内空間に放散する。 また塔内の液溜りから送水ポンプ8を経て圧送されたオ
ゾン化水は流量制御弁11を通じて上下各段のスプレー
ノズル群7a、 7bへ供給され、塔内の下部領域には
微細水滴粒子のシャワーBbが、上部領域には粗大水滴
粒子のシャワーBaが分散噴霧される。この状態で図示
されてない室から抽気された塵埃、@を含むlη染空気
流は送風機3.プレフィルタ4を通して水洗塔5の塔内
空間へ下方から導入されて矢印Aのように塔内を上昇し
て流れ、この上昇過程で塔内のオゾン雰囲気による殺菌
作用を受けるとともに、前記した水滴粒子の噴霧シャワ
ーと対流接触して空気流中に含まれている塵埃、菌が補
集分離される。この場合にまず空気流はスプレーノズル
群7bより噴霧して塔内の下部領域に充満している微細
な水滴粒子と効率よく接触し、空気流に含まれている塵
埃、菌等が水滴粒子に移行して補集される。 同時にこの領域の上方には上段側のスプレーノズル7a
から粗大な水滴粒子のシャワーが噴霧されており、空気
流とともに塔内を上昇浮上してくる塵埃、閏を採り込ん
だ微細水滴粒子は粗大な水滴粒子に捕捉され、空気流A
に逆らって下方へ重力沈降して塔内底部に溜るようにな
る。一方、塔内で洗浄水の噴霧シャワー領域を通過した
空気流は塔内設置のエリミネータ16、および後段の除
滴サイクロン17で微細な水滴粒子が、また活性炭フィ
ルタ18でオゾンが除去された後に、第2図に示した空
調装置を経て再び室内に送気還流される。なお水洗塔5
内の底部に溜っている洗浄水は水位が常時監視され塔内
水位が所定水位より低下すると水位調節弁13を通じて
上水が補給される。 上記した除塵、除菌装置の性能評価を確認するために本
発明者が行った実験結果によれば、粒径側の除塵効率は
2.0μm以上で100%、1.0μm以上では99.
8%、0.5μm以上では98.7%、0.2μm以上
では94.2%の良好な集塵効率が得られ、かつ図示装
置を経由して清浄化された空気流および洗浄塔内に溜っ
ている洗浄水ともにオゾンによる殺菌作用で充分に滅菌
処理されていることが確認されている。
FIG. 1 shows an embodiment of the invention, and the same members corresponding to FIG. 2 are given the same reference numerals. That is, according to the present invention, in the washing water circulation supply system provided in the washing tower 5, the water spray nozzles installed in the tower are divided into upper and lower spray nozzle groups 7a and 7b. Here, the spray nozzle group 7b on the lower stage has a small diameter spray nozzle and sprays a shower of fine water droplets of about 200 μI, whereas the spray nozzle group 7a on the upper stage has coarse water droplets with a diameter of about 500 μI. Consists of a nozzle configured to generate a shower. In addition, 11 is a flow control valve inserted in the branch pipe to the spray nozzle group of each stage, 12 is the water supply pipe that replenishes washing water into the tower, and 13 is a control valve for the water level in the tower inserted in the same pipe. It is. The water washing tower 5 is also equipped with ozone supply means consisting of an ozonizer 14 that generates ozone as a disinfectant, and an ozone supply nozzle 15 as a bubble generator pulled out from the ozonizer 14 and placed in the bottom liquid pool of the water washing tower 5. has been done. In addition, on the exhaust side of the water washing tower 5, there is an eliminator 16 for removing water droplets at the upper part of the inside of the water washing tower 5 as a drip removal means, and a drip removing cyclone 17 for removing water droplets is installed at the rear stage of the water washing tower 5. An activated carbon filter 18 is installed to remove ozone. Note that 19 is a filter for cleaning waste water inserted in the drain pipe line. Next, the operation of the above configuration will be explained. During operation, ozone generated by the ozonizer 14 is supplied to the ozone supply nozzle 15.
The ozone bubbles C become ozone bubbles C and are discharged and supplied into the washing water accumulated at the bottom of the washing tower 5, a part of which dissolves in the water, and the rest rises in the water as bubbles and is dissipated into the space inside the tower. Further, the ozonated water that is pressure-fed from the liquid reservoir in the tower via the water supply pump 8 is supplied to the spray nozzle groups 7a and 7b in the upper and lower stages through the flow control valve 11, and a shower of fine water droplets is created in the lower region of the tower. Bb is dispersed and a shower of coarse water droplets Ba is sprayed in the upper region. In this state, the lη-stained air flow containing dust and @ extracted from a room (not shown) is sent to the blower 3. It is introduced from below into the internal space of the water washing tower 5 through the pre-filter 4 and flows upward within the tower as shown by arrow A. During this ascending process, it is subjected to the sterilizing effect of the ozone atmosphere within the tower, and the water droplet particles described above are Dust and bacteria contained in the air stream are collected and separated by convection contact with the spray shower. In this case, first, the air stream is sprayed from the spray nozzle group 7b and efficiently contacts the fine water droplets filling the lower area of the tower, and the dust, bacteria, etc. contained in the air stream become the water droplets. Transferred and collected. At the same time, above this area is the upper spray nozzle 7a.
A shower of coarse water droplets is sprayed from the air stream, and the fine water droplets that incorporate dust and particles that rise up and float up in the tower with the airflow are captured by the coarse water droplets, and the airflow A
It sinks downward due to gravity and accumulates at the bottom of the tower. On the other hand, the airflow that has passed through the spray shower area of washing water inside the tower is removed by an eliminator 16 installed inside the tower and a subsequent drip-removal cyclone 17 to remove fine water droplets, and an activated carbon filter 18 to remove ozone. The air is sent back into the room via the air conditioner shown in FIG. 2. In addition, water washing tower 5
The water level of the washing water stored at the bottom of the tower is constantly monitored, and when the water level in the tower drops below a predetermined water level, clean water is replenished through the water level control valve 13. According to the results of experiments conducted by the present inventor to confirm the performance evaluation of the above-mentioned dust removal and sterilization equipment, the dust removal efficiency on the particle size side is 100% for particles of 2.0 μm or more, and 99% for particles of 1.0 μm or more.
A good dust collection efficiency of 8%, 98.7% for 0.5 μm or more, and 94.2% for 0.2 μm or more was obtained, and the purified air flow through the illustrated device and the cleaning tower It has been confirmed that the accumulated cleaning water has been sufficiently sterilized by the sterilization effect of ozone.

【発明の効果】【Effect of the invention】

以上述べたようにこの発明によれば、水洗塔内に上下段
に分割配備されてその下段側からは微細水滴粒子、上段
側からは粗大水滴粒子のシャワーを汚染気体に向けて噴
霧するスプレーノズルを含む洗浄水の循環供給系と、塔
内底部の液溜りの水中に殺菌剤としてのオゾンを供給す
るオゾン供給手段と、水洗塔の排気側に設置した水滴除
手段およびオゾン除去手段とを具備して構成したことに
より、コンパクトな構成で汚染気体中に含まれている微
少な塵埃、Wを効果的に分離補集して高い除塵、除菌効
率が得られるとともに、同時にオゾンの殺凹作用により
水洗塔内を流れる空気流中の菌および塔内で分離補集さ
れた菌を滅菌処理でき、かくして綜合的な気体清浄効果
の高い除塵・除菌装置を得ることができる。
As described above, according to the present invention, the spray nozzle is divided into upper and lower stages in the water washing tower, and sprays a shower of fine water droplets from the lower stage and coarse water droplets from the upper stage toward the contaminated gas. A cleaning water circulation supply system containing water, an ozone supply means for supplying ozone as a disinfectant into the water in the liquid pool at the bottom of the tower, and a water droplet removal means and an ozone removal means installed on the exhaust side of the water washing tower. With this structure, it is possible to effectively separate and collect fine dust and W contained in contaminated gas with a compact structure, resulting in high dust removal and sterilization efficiency, and at the same time, the sterilizing effect of ozone can be achieved. This makes it possible to sterilize bacteria in the airflow flowing through the water washing tower and bacteria separated and collected within the tower, thus providing a dust removal and sterilization device with a high comprehensive gas cleaning effect.

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

第1図はこの発明の実施例の構成配置図、第2図は従来
における一般的な除塵・#、菌装置のシステム図である
1図において、 2:気体の循環送風路、3:送風機、5:水洗塔、7a
:粗大水滴粒子噴霧用のスプレーノズル、7b:i細水
滴粒子噴霧用のスプレーノズル、14:オゾナイザ、1
5ニオシン供給ノズル、16:除滴用のエリミネータ、
エフ:除滴サイクロン、18ニオシン除去用の活性炭フ
ィルタ、A:汚染空気流、Ba。 Bb、洗浄水の噴霧シャワー、Cニオシン。 ]O 第2図
Fig. 1 is a configuration diagram of an embodiment of the present invention, and Fig. 2 is a system diagram of a conventional general dust removal/bacteria device. 5: Washing tower, 7a
: spray nozzle for spraying coarse water droplets, 7b: i spray nozzle for spraying fine water droplets, 14: ozonizer, 1
5 Niosin supply nozzle, 16: Eliminator for drip removal,
F: Drip removal cyclone, activated carbon filter for removing 18 niosine, A: Contaminated air flow, Ba. Bb, spray shower of wash water, C niosin. ]O Figure 2

Claims (1)

【特許請求の範囲】[Claims] 1)塵埃、菌を含む汚染気体を水洗塔内に導入し、該水
洗塔内で気体に水を噴霧することにより気体から塵埃、
菌を分離補集して汚染気体を清浄化する気体の除塵・除
菌装置において、前記水洗塔内に上下段に分割配備され
てその下段側からは微細水滴粒子、上段側からは粗大水
滴粒子のシャワーを汚染気体に向けて噴霧するスプレー
ノズルを含む洗浄水の循環供給系と、塔内底部の液溜り
の水中に殺菌剤としてのオゾンを供給するオゾン供給手
段と、水洗塔の排気側に設置した水滴除手段およびオゾ
ン除去手段とを具備して構成したことを特徴とする気体
の除塵・除菌装置。
1) Contaminated gas containing dust and bacteria is introduced into a water washing tower, and water is sprayed onto the gas in the washing tower to remove dust and bacteria from the gas.
In a gaseous dust removal and sterilization device that separates and collects bacteria to purify contaminated gas, the water washing tower is divided into upper and lower stages, with fine water droplets from the lower stage and coarse water droplets from the upper stage. A washing water circulation supply system including a spray nozzle that sprays a shower of water toward contaminated gas, an ozone supply means that supplies ozone as a disinfectant into the water in the liquid pool at the bottom of the tower, and an ozone supply system on the exhaust side of the washing tower. 1. A gaseous dust removal and sterilization device comprising a water droplet removal means and an ozone removal means installed.
JP60207584A 1985-09-19 1985-09-19 Dust and germ removing device for gas Granted JPS6269033A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60207584A JPS6269033A (en) 1985-09-19 1985-09-19 Dust and germ removing device for gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60207584A JPS6269033A (en) 1985-09-19 1985-09-19 Dust and germ removing device for gas

Publications (2)

Publication Number Publication Date
JPS6269033A true JPS6269033A (en) 1987-03-30
JPH0325702B2 JPH0325702B2 (en) 1991-04-08

Family

ID=16542178

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60207584A Granted JPS6269033A (en) 1985-09-19 1985-09-19 Dust and germ removing device for gas

Country Status (1)

Country Link
JP (1) JPS6269033A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02135110A (en) * 1988-11-16 1990-05-24 Daiei Sangyo Kk Purifying treatment of polluted air and its apparatus
EP1816409A2 (en) * 2006-02-01 2007-08-08 Sanyo Electric Co., Ltd. Air filtering apparatus and control method therefor
EP1890089A2 (en) * 2006-08-07 2008-02-20 SANYO ELECTRIC Co., Ltd. air filtering apparatus
EP1891980A3 (en) * 2006-08-21 2009-07-29 Sanyo Electric Co., Ltd. Air filtering apparatus
JP2011094843A (en) * 2009-10-28 2011-05-12 Ihi Corp Condenser
US20170010044A1 (en) * 2013-12-11 2017-01-12 Starklab Device for producing a stream of air through a volume of liquid
US20170320006A1 (en) * 2014-11-06 2017-11-09 Starklab Device for producing and treating a gas stream through a volume of liquid, and facility and method implementing said device
IT202000012268A1 (en) * 2020-05-25 2021-11-25 Starpool S R L VENTILATION AND SANITIZATION SYSTEM FOR CONFINED ROOMS FOR SPAS, PARTICULARLY FOR SAUNAS, SPAS AND TURKISH BATHS

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02135110A (en) * 1988-11-16 1990-05-24 Daiei Sangyo Kk Purifying treatment of polluted air and its apparatus
EP1816409A2 (en) * 2006-02-01 2007-08-08 Sanyo Electric Co., Ltd. Air filtering apparatus and control method therefor
EP1816409A3 (en) * 2006-02-01 2010-10-13 Sanyo Electric Co., Ltd. Air filtering apparatus and control method therefor
EP1890089A2 (en) * 2006-08-07 2008-02-20 SANYO ELECTRIC Co., Ltd. air filtering apparatus
US7896947B2 (en) 2006-08-07 2011-03-01 Sanyo Electric Co., Ltd. Air filtering apparatus
EP1890089A3 (en) * 2006-08-07 2009-10-14 SANYO ELECTRIC Co., Ltd. air filtering apparatus
US7857897B2 (en) 2006-08-21 2010-12-28 Sanyo Electric Co., Ltd. Air filtering apparatus
EP1891980A3 (en) * 2006-08-21 2009-07-29 Sanyo Electric Co., Ltd. Air filtering apparatus
JP2011094843A (en) * 2009-10-28 2011-05-12 Ihi Corp Condenser
US20170010044A1 (en) * 2013-12-11 2017-01-12 Starklab Device for producing a stream of air through a volume of liquid
US11035614B2 (en) * 2013-12-11 2021-06-15 Starklab Device for producing a stream of air through a volume of liquid
US20170320006A1 (en) * 2014-11-06 2017-11-09 Starklab Device for producing and treating a gas stream through a volume of liquid, and facility and method implementing said device
US10946326B2 (en) * 2014-11-06 2021-03-16 Starklab Device for producing and treating a gas stream through a volume of liquid, and facility and method implementing said device
US11452965B2 (en) 2014-11-06 2022-09-27 Starklab Device for producing and treating a gas stream through a volume of liquid, and facility and method implementing said device
IT202000012268A1 (en) * 2020-05-25 2021-11-25 Starpool S R L VENTILATION AND SANITIZATION SYSTEM FOR CONFINED ROOMS FOR SPAS, PARTICULARLY FOR SAUNAS, SPAS AND TURKISH BATHS

Also Published As

Publication number Publication date
JPH0325702B2 (en) 1991-04-08

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