JPH0325702B2 - - Google Patents

Info

Publication number
JPH0325702B2
JPH0325702B2 JP60207584A JP20758485A JPH0325702B2 JP H0325702 B2 JPH0325702 B2 JP H0325702B2 JP 60207584 A JP60207584 A JP 60207584A JP 20758485 A JP20758485 A JP 20758485A JP H0325702 B2 JPH0325702 B2 JP H0325702B2
Authority
JP
Japan
Prior art keywords
water
tower
ozone
dust
washing tower
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP60207584A
Other languages
Japanese (ja)
Other versions
JPS6269033A (en
Inventor
Kyokatsu Ueda
Akira Ishikawa
Takeo Takahashi
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

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、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、除菌を行つて清浄化するよう
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 purifies indoor air by removing dust and sterilization from food processing rooms, food storage rooms, hospital operating rooms, 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、該室1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3、粗大な塵埃を除去するプレフイルタ4、水
洗塔5、および空調装置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
フイルタ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捕集され、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
に空調装置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
に溜つた水は活性炭、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10
は定期的に塔内の洗浄水を交換する際に洗浄廃水
を系外に排出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
を受け易くなり、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に水洗塔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
れなかつた空気流中の菌が生存したまま空気流に
乗つて水洗塔5から下流側へ逸出する他、水洗塔
内で補集された菌が液溜りに滞留している水中で
繁殖し、噴霧シヤワー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
棄処理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 blowing passage 2 is constructed between the air intake port and the air supply port of the room 1, and a blower 3, A prefilter 4 for removing coarse dust, a water washing tower 5, and an air conditioner 6 are installed in order,
These make up the dust removal and sterilization device system. Here, the water washing tower 5 is configured as a spray type washing dust collector equipped with a water spray system that connects a spray nozzle 7 for spraying minute water droplets into the tower, a water pump 8, a water filter 9, etc. ing. 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 prefilter 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 adhering to the tower are transferred to water droplets due to the cleaning and dust collection action, separated and collected from the air flow, and settle in the tower and accumulate at the bottom. On the other hand, the air stream that has been purified by dust removal and sterilization is discharged from the upper part of the tower, and after the temperature and humidity are adjusted by the air conditioner 6, it 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. Note 10
is a drain valve that discharges washing waste water out of the system when the washing 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 and the water droplet particles B dispersed and sprayed into the tower from the spray nozzle 7 are used.
It is necessary to increase the collection rate of dust and bacteria by increasing the contact ratio and the relative speed of collision. 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 diameter 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 rise inside the tower while taking in dust and bacteria. Washing tower 5 is carried by the air flow
The proportion of particles escaping to the outside increases, and if this continues, dust removal and sterilization efficiency will decrease. On the other hand, in order to prevent such water droplets from escaping outside the tower, it is possible to consider means of lowering the wind speed of the air flowing inside the tower. This results in the problem of increasing the size of the 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. Not equipped with means to sterilize
If this continues, the bacteria in the airflow that could not be completely 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, and will also be collected inside the washing tower. The problem remains that bacteria breed in the water that remains in the liquid pool, increasing the degree of bacterial contamination of the spray shower. In this case, it is conceivable to frequently discharge the washing water to the outside of the system, disinfect and sterilize this wastewater, and then treat it as wastewater. However, in a large-capacity washing tower, the amount of washing water used for spraying is large, and Disposing of the waste increases the consumption of washing water and increases operating costs.

【発明の目的】[Purpose of the invention]

この発明は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 was developed in consideration of the above points, and it eliminates the drawbacks of the conventional device described above, has a small structure, has high dust removal and sterilization efficiency, and is a gas-based device that can sterilize bacteria. The purpose is to provide comprehensive cleaning performance and highly reliable dust removal and sterilization equipment.

【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ヤワ
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
塵埃流子、菌の補集効率を高めつつ、塔内の上部
領域では下方から上昇通流する気体流と一緒に浮
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
噴霧シヤワーの間隙を縫つ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、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 has 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 a shower of coarse water droplets from the upper stage toward 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. It was constructed as follows. With this configuration, firstly, in the lower region of the water washing tower, sufficient contact between fine water droplets and the contaminated gas flow introduced into the tower increases the efficiency of scavenging dust droplets and bacteria in the contaminated gas flow by the water droplets. At the same time, in the upper region of the tower, fine water droplets that rise together with the gas flow flowing upward from below are captured by coarse water droplets and allowed to settle downward by gravity. As a result, fine water droplets that tend to flow out of the tower downstream together with the airflow can be reliably removed from the airflow by the droplet removal means, and even higher dust removal and sterilization efficiency can be obtained. 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て
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200μm前後の微細水滴粒子シヤワーを
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500μm前後の粗大水滴
粒子シヤ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の後退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イルタ1
8が設置されている。なお19はドレン排水管路
に介装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となつて洗浄塔
5の塔内底部に溜つ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ヤワーBbが、上部領域に
は粗大水滴粒子のシヤワーBaが分散噴霧される。
この状態で図示されていない室から抽気された塵
埃、菌を含む汚染空気流は送風機3、プレフイル
タ4を通じて水洗塔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ヤワ
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
子のシヤ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、菌を採り込んだ微
細水滴粒子は粗大な水滴粒子に捕捉され、空気流
Aに逆らつ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ヤワー
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、また活性炭フイルタ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
部に溜つ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つた実験結果によれば、粒径
別の除塵効率は2.0μm以上100%、1.0μm以上で
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
溜つ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 this invention,
Identical parts 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 side is a nozzle that has a small diameter spray nozzle and sprays fine water droplet shower particles of around 200 μm, whereas the spray nozzle group 7a on the upper side sprays coarse water droplet particles around 500 μm in diameter. It consists of a nozzle set to generate. 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, water washing tower 5
On the exhaust side of the water washing tower 5, an eliminator 16 for removing water droplets is installed at the upper part 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 of the water washing tower 5, and an activated carbon filter for removing ozone from the gas. 1
8 is installed. Note that 19 is a filter for cleaning waste water that is installed in the drain pipe line. Next, the operation of the above configuration will be explained. During operation, ozone generated by the ozonizer 14 is turned into ozone bubbles C from the ozone supply nozzle 15 and is discharged and supplied into the cleaning water accumulated at the bottom of the cleaning tower 5. A part of the ozone is dissolved in the water and the rest is bubbles. It rises through the water and dissipates 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 rate control valve 11, and the lower region of the tower is showered with fine water droplets. Bb is dispersed and sprayed with a shower of coarse water droplets Ba in the upper region.
In this state, a flow of contaminated air containing dust and bacteria is extracted from a room (not shown) and is introduced from below into the interior space of the water washing tower 5 through the blower 3 and prefilter 4, and rises inside the tower as shown by arrow A. During this rising process, the ozone atmosphere inside the tower receives a sterilizing action, and the dust contained in the air flow is removed by convection contact with the atomized shower of water droplets.
Bacteria are collected and separated. 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, a shower of coarse water droplets is being sprayed above this area from the spray nozzle 7a on the upper stage side, and the fine water droplets that have taken in dust and bacteria that rise up in the tower with the airflow are coarse. The water is captured by the water droplets, sinks downward by gravity against the airflow A, and accumulates at the bottom of the tower. On the other hand, the airflow that has passed through the washing water spray shower area in 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. The water level of the washing water stored at the bottom of the washing tower 5 is constantly monitored, and when the water level in the tower falls below a predetermined water level, clean water is replenished through the water level control valve 13. According to the experimental results conducted by the present inventor to confirm the performance evaluation of the above-mentioned dust removal and sterilization equipment, the dust removal efficiency by particle size is 100% for particles of 2.0 μm or more, and 100% for particles of 1.0 μm or more.
99.8%, 98.7% for 0.5μm or more, 0.2μm or more
A good dust collection efficiency of 94.2% was obtained, and both the air flow purified through the illustrated device and the washing water accumulated in the washing tower were sufficiently sterilized by the sterilization effect of ozone. Confirmed.

【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ヤワー
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、菌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
ンの殺菌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 a water washing tower, and sprays fine water droplets from the lower stage and coarse water droplets from the upper stage towards 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 compact configuration, it is possible to effectively separate and collect fine dust and bacteria contained in contaminated gas, resulting in high dust removal and sterilization efficiency, and at the same time, the sterilization effect of ozone Bacteria in the air flowing through the water washing tower as well as bacteria separated and collected within the tower can be sterilized, resulting in dust removal and
A sterilization device can be obtained.

【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・除菌装置のシス
テム図である。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:微細水滴粒子噴霧用のスプレーノズ
ル、14:オゾナイザ、15:オゾン供給ノズ
ル、16:除滴用のエリミネータ、17:除滴サ
イクロン、18:オゾン除去用の活性炭フイル
タ、A:汚染空気流、Ba,Bb:洗浄水の噴霧シ
ヤワー、C:オゾン。
Fig. 1 is a configuration diagram of an embodiment of this invention;
The figure is a system diagram of a conventional general dust removal and sterilization device. In the figure, 2: gas circulation air passage, 3: blower, 5: water washing tower, 7a: spray nozzle for spraying coarse water droplets, 7b: spray nozzle for spraying fine water droplets, 14: ozonizer, 15: ozone supply Nozzle, 16: Eliminator for drip removal, 17: Drop removal cyclone, 18: Activated carbon filter for ozone removal, A: Contaminated air flow, Ba, Bb: Cleaning water spray shower, C: Ozone.

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ヤ
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. Dust removal of gas, in which 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 separate and collect dust and bacteria from the gas and purify the contaminated gas. In the sterilization device, the cleaning water is divided into upper and lower stages in the water washing tower, and includes spray nozzles that spray fine water droplets from the lower stage and coarse water droplets from the upper stage toward the contaminated gas. It is configured to include a circulation supply system, 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. A gaseous dust removal and sterilization device featuring:
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 JPS6269033A (en) 1987-03-30
JPH0325702B2 true 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)

Families Citing this family (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
JP4878855B2 (en) * 2006-02-01 2012-02-15 三洋電機株式会社 Air sterilization apparatus and control method
CA2593954C (en) 2006-08-07 2011-01-04 Sanyo Electric Co., Ltd. Air filtering apparatus
JP4928869B2 (en) * 2006-08-21 2012-05-09 三洋電機株式会社 Air sanitizer
JP5531557B2 (en) * 2009-10-28 2014-06-25 株式会社Ihi Capacitor
FR3014548B1 (en) * 2013-12-11 2018-11-30 Starklab PROVIDING THE PRODUCTION OF AN AIR FLOW WHOSE TEMPERATURE IS CONTROLLED BY THERMAL EXCHANGE WITH A LIQUID AND WITH DIRECT CONTACT OF THE AIR FLOW AND THE FLUID
MA40912A (en) * 2014-11-06 2017-09-12 Starklab DEVICE FOR THE PRODUCTION AND TREATMENT OF A GAS FLOW THROUGH A VOLUME OF LIQUID, INSTALLATION AND PROCESS IMPLEMENTING THIS 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
JPS6269033A (en) 1987-03-30

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