JPH0518609B2 - - Google Patents

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Publication number
JPH0518609B2
JPH0518609B2 JP62104742A JP10474287A JPH0518609B2 JP H0518609 B2 JPH0518609 B2 JP H0518609B2 JP 62104742 A JP62104742 A JP 62104742A JP 10474287 A JP10474287 A JP 10474287A JP H0518609 B2 JPH0518609 B2 JP H0518609B2
Authority
JP
Japan
Prior art keywords
water tank
section
air
cooling
cooling water
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
JP62104742A
Other languages
Japanese (ja)
Other versions
JPS63270521A (en
Inventor
Yukio Ozaki
Kozo Shinba
Yoshinobu Matsushita
Hiromitsu Ooike
Akyori Oono
Kunihiko Myamoto
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.)
Nippon Light Metal Co Ltd
Original Assignee
Nippon Light Metal 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 Nippon Light Metal Co Ltd filed Critical Nippon Light Metal Co Ltd
Priority to JP62104742A priority Critical patent/JPS63270521A/en
Publication of JPS63270521A publication Critical patent/JPS63270521A/en
Publication of JPH0518609B2 publication Critical patent/JPH0518609B2/ja
Granted legal-status Critical Current

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  • Separation Of Particles Using Liquids (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は湿式空気清浄装置に関するもので、
更に詳細には、例えば食品、薬品又は精密機械、
半導体等の大工場用のクリーンルーム、事務所あ
るいは病院等の室内の空気中の塵埃を液滴流動域
を利用して除去すると共に湿度・温度調節して、
再び室内に循環することを目的とする湿式空気清
浄装置に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] This invention relates to a wet air cleaning device.
More specifically, for example, food, medicine or precision machinery,
It uses a droplet flow area to remove dust from the air in clean rooms for large semiconductor factories, offices, hospitals, etc., and also adjusts humidity and temperature.
The present invention relates to a wet air purifying device whose purpose is to circulate the air indoors again.

[従来の技術] 従来のこの種の空気清浄装置としては、第23
図に示すように、送風機aを介して室bの出口c
と接続する蒸発器eと、パイプfを介して室bの
入口dに接続する加温器gとを接続し、また、蒸
発器e内に蛇行状に配備される冷媒蒸発管hの出
入口をそれぞれ冷媒供給管i及び冷媒排出管jを
介して冷凍機kに接続すると共に、加温器g内に
蛇行状に配備される冷媒凝縮管の出入口をパイプ
m、nを介して冷凍機kに接続した構造のもの、
あるいは、第24図に示すように、上記蒸発器e
に変えてサイクロン型の蒸発器e′を使用し、上記
加温器gに変えてサイクロン型の加温器g′を使用
した逆ランキンサイクルのものが知られている
(特開昭59−185922号参照)。
[Prior art] As a conventional air purifying device of this type, the 23rd
As shown in the figure, outlet c of chamber b via blower a
The evaporator e is connected to the inlet d of the chamber b via the pipe f, and the heater g is connected to the inlet d of the chamber b via the pipe f. It is connected to the refrigerator k through a refrigerant supply pipe i and a refrigerant discharge pipe j, respectively, and the entrance and exit of the refrigerant condensing pipe arranged in a meandering manner in the warmer g is connected to the refrigerator k through pipes m and n. connected structures,
Alternatively, as shown in FIG. 24, the evaporator e
A reverse Rankine cycle is known in which a cyclone-type evaporator e' is used instead of the heater g, and a cyclone-type warmer g' is used instead of the warmer g (Japanese Patent Laid-Open No. 59-185922). (see issue).

上記のように構成される従来の空気清浄装置に
おいて、上記送風機aによつて室bから蒸発器
e、e′内に吹込まれた空気は、微細水滴(冷水微
細ミスト)と接触して飽和温度に調湿されると共
に、蒸発器e内において水シヤワーによつて空気
中の塵埃、細菌、ウイルス等の有害成分が除去さ
れる。そして、冷却加湿された空気は加温器g内
に送込まれて加温器g、g′内において適温加温さ
れると共に調湿された後、室b内に循環されるよ
うになつている。
In the conventional air purifying device configured as described above, the air blown into the evaporators e and e' from the chamber b by the blower a comes into contact with fine water droplets (cold water fine mist) and reaches a saturation temperature. At the same time, harmful components such as dust, bacteria, and viruses in the air are removed by a water shower in the evaporator e. The cooled and humidified air is then sent into the warmer g, where it is heated to an appropriate temperature and humidity-controlled, and then circulated into the room b. There is.

[発明が解決しようとする問題点] しかしながら、従来の空気清浄装置において
は、空気中の塵埃と冷水微細ミストとの接触、冷
却及び加熱を別々の機器にて行うため、各機器を
別々に用意する必要があると共に、それらの配管
や全体の系路が長大化し、また、空気を送る送風
設備も大型又は多数化するため、構造全体が大型
かつ複雑化すると共に、施工工数がかかりコスト
が嵩むという問題があつた。
[Problems to be solved by the invention] However, in conventional air purifying devices, the contact between dust in the air and the fine mist of cold water, cooling, and heating are performed using separate devices, so each device must be prepared separately. At the same time, the piping and overall system routes become longer, and the blower equipment that sends the air also becomes larger or more numerous, making the entire structure larger and more complex, requiring more man-hours for construction, and increasing costs. There was a problem.

[問題点を解決するための手段] この発明は上記事情に鑑みなされたもので、上
記技術的課題を解決するために、第1の発明は、
清浄及び調温・調湿化されるべき空気中の塵埃、
細菌等を荷電させる荷電部と、これら塵埃等に冷
水微細ミストを接触する冷水供給部と、冷却され
た塵埃等を捕集する冷却捕集部及び微細水滴除去
部と、清浄化された空気を調温・調湿するための
再熱手段を一箇所に集合して、効率良く空気の清
浄化及び調温・調湿化を行うと共に、塵埃の捕集
を効率よく行うことができるようにしたことを特
徴とし、また、第2の発明は、上記第1発明に加
えて、更に、冷水供給部に供給される冷却水を殺
菌処理する手段を付加したことを特徴とする湿式
空気清浄装置を提供しようとするものである。
[Means for Solving the Problems] This invention was made in view of the above circumstances, and in order to solve the above technical problems, the first invention is as follows:
Dust in the air that should be cleaned and temperature/humidity controlled;
A charging section that charges bacteria, etc., a cold water supply section that brings a fine mist of cold water into contact with the dust, a cooling collection section and a fine water droplet removal section that collect the cooled dust, etc., and a part that supplies purified air. Reheating means for controlling temperature and humidity are gathered in one place, making it possible to efficiently purify the air and control temperature and humidity, as well as efficiently collect dust. A second invention is a wet air purifying device characterized in that, in addition to the first invention, a means for sterilizing the cooling water supplied to the cold water supply section is further added. This is what we are trying to provide.

すなわち、第1の発明は、下部又は別個に温度
調整手段により温度調整される水を収容する冷却
水槽を設け、かつ、その上部側方に空気流入口を
開口すると共に、上部に空気流出口を開口する筒
状の空気清浄装置本体と、上記空気清浄装置本体
内の空気流入口と空気流出口の中間部に配設され
る冷水供給部と、上記冷水供給部の下方上流側に
水平状に配設される冷却捕集部と、上記冷水供給
部の上方下流側に向つて順次配設される微細水滴
除去部及び再熱手段とを備え、上記空気流入口の
上流側に荷電部を設けると共に、送風手段を介し
て室の吸込口に接続し、上記空気流出口を上記室
の吹出口に接続して成り、上記冷却捕集部が、多
孔板と、この多孔板の下面に配設されるハニカム
コア体とで構成される1組又は複数組の捕集体で
あり、上記荷電部が、複数の透孔を穿設する放電
対極と、上記各透孔の中心に位置する複数の先尖
状放電針を突設する放電極とで構成されると共
に、上記冷却捕集部が、上記荷電部の放電極と反
対極に通電されて成ることを特徴とする湿式空気
清浄装置を提供し、また、第2の発明は、上記湿
式空気清浄装置において、上記冷却水槽内冷却水
を殺菌処理する殺菌手段を付加して成ることを特
徴とする湿式空気清浄装置を提供しようとするも
のである。
That is, the first invention provides a cooling water tank for accommodating water whose temperature is adjusted by a lower part or a separate temperature adjustment means, and an air inlet is opened on the side of the upper part, and an air outlet is provided in the upper part. A cylindrical air purifier main body that opens, a cold water supply section disposed at an intermediate portion between the air inlet and the air outlet in the air purifier main body, and a horizontally arranged water supply section located below and upstream of the cold water supply section. a cooling collection section disposed; a fine water droplet removing section and a reheating means disposed in sequence toward the upper downstream side of the cold water supply section; and a charging section provided upstream of the air inlet. and the air outlet is connected to the air inlet of the chamber via an air blowing means, and the air outlet is connected to the air outlet of the chamber, and the cooling collection section is provided with a perforated plate and a lower surface of the perforated plate. one or more sets of collecting bodies, each consisting of a honeycomb core body in which the charging section has a plurality of through holes, a discharge counter electrode having a plurality of through holes, and a plurality of tips located at the center of each of the through holes; Provided is a wet air purifying device comprising a discharge electrode having a pointed discharge needle protruding therefrom, and wherein the cooling collection section is energized to a polarity opposite to the discharge electrode of the charging section. A second aspect of the present invention is to provide a wet air purifying device characterized in that the wet air purifying device further includes a sterilizing means for sterilizing the cooling water in the cooling water tank. .

この発明において、上記温度調整手段は冷却水
槽内に収容される冷却水を所定の温度に冷却する
ものであれば任意のものであつてもよいが、好ま
しくは冷却水槽の上部又は冷却水槽内に配設され
る冷却コイルにて形成する方がよい。
In this invention, the temperature adjusting means may be any means as long as it cools the cooling water contained in the cooling water tank to a predetermined temperature, but is preferably installed at the top of the cooling water tank or within the cooling water tank. It is better to form the cooling coil provided.

上記冷却捕集部は、多孔板と、この多孔板の下
面に配設されるハニカムコア体とで構成される捕
集体であれば任意のものであつてもよいが、好ま
しくは複数組の捕集体にて形成する方がよく、か
つ、ハニカムコア体は、その透孔同士が互いに偏
倚する複数の積層されたハニカムコア素材にて構
成する方がよい。
The cooling collection unit may be any collection body as long as it is composed of a perforated plate and a honeycomb core body disposed on the lower surface of the perforated plate, but it is preferable to use a plurality of sets of collection units. It is better to form the honeycomb core body as an aggregate, and it is better to construct the honeycomb core body from a plurality of laminated honeycomb core materials whose through holes are offset from each other.

更に、第2の発明において、上記殺菌手段は例
えば紫外線殺菌装置等冷却水槽内の水を殺菌処理
する手段であれば任意のものであつてもよいが、
好ましくはオゾンによる殺菌手段である方がよ
い。この場合、殺菌手段の一部を構成するオゾン
発生器は冷却水槽又は冷却水槽に接続する水槽内
に配設されるオゾン曝気部にオゾンを供給する外
部配置式のもののほか、上記いずれかの水槽内に
配設される酸化チタン製被照射体と、この被照射
体に光を照射する発光体とで構成される内部設置
式のもののいずれであつてもよい。
Furthermore, in the second invention, the sterilizing means may be any means for sterilizing water in the cooling water tank, such as an ultraviolet sterilizer, but
It is preferable to use ozone as a sterilization means. In this case, the ozone generator that constitutes part of the sterilization means may be an external type that supplies ozone to the ozone aeration section installed in the cooling water tank or the water tank connected to the cooling water tank, or an external type that supplies ozone to the ozone aeration section installed in the cooling water tank or the water tank connected to the cooling water tank. It may be any type of internally installed type consisting of a titanium oxide irradiated object disposed inside and a light emitter that irradiates the irradiated object with light.

[作用] 上記技術的手段は次のように作用する。[Effect] The above technical means works as follows.

送風手段の駆動により室内の汚染された空気が
空気清浄装置本体内に送られる際、まず、荷電部
にて汚染空気中の塵埃が帯電される。次に、汚染
空気が冷却捕集部を通過する際、冷水供給部から
冷水が散布されて冷水捕集部の多孔板上に供給さ
れ、上昇してくる汚染空気と接触する。したがつ
て、流下する冷水と上昇する汚染空気とは同時に
多孔板の目孔を通過することになる。汚染空気は
多孔板の目孔を通過する時、多孔板の目孔に張つ
た液膜を激しく破りながら、微細な液滴と微細な
気泡を生成する。その結果、多孔板上には粉体の
流動層に酷似した濃密な液滴流動域が、汚染空気
圧損と均衡して適当な厚みで形成される。
When the indoor contaminated air is sent into the main body of the air purifier by driving the blowing means, first, the dust in the contaminated air is charged by the charging section. Next, when the contaminated air passes through the cooling collection section, cold water is sprayed from the cold water supply section and supplied onto the perforated plate of the cold water collection section, where it comes into contact with the rising contaminated air. Therefore, the cold water flowing down and the contaminated air rising will pass through the holes in the perforated plate at the same time. When the contaminated air passes through the holes in the perforated plate, it violently breaks the liquid film that has formed in the holes in the perforated plate, generating minute droplets and minute bubbles. As a result, a dense droplet flow region closely resembling a fluidized bed of powder is formed on the porous plate with an appropriate thickness in balance with the pressure loss of the contaminated air.

汚染空気中の塵埃、細菌は、多孔板の目孔に張
つた液膜を破る時、及び多孔板上に形成される液
滴流動域が通過する際に、効果的な気−液接触が
行われ、有害塵埃等は十分液側に移行され、捕集
される。
Dust and bacteria in contaminated air undergo effective gas-liquid contact when they break through the liquid film stretched over the holes of the perforated plate and when the droplet flow area formed on the perforated plate passes through. However, harmful dust and other particles are sufficiently transferred to the liquid side and collected.

しかも、冷却捕集部を構成する捕集体が多孔板
の下面にハニカムコア体を配設して成るので、ハ
ニカムコア体のセル内壁を流下する液膜にも塵埃
等が接触捕集され、更に、複数の透孔を穿設する
放電対極と、各透孔の中心に位置する複数の先尖
状放電針を突設する放電極とで荷電部を構成する
ことにより塵埃等の帯電効率を高くすることに加
え、冷却捕集部が荷電部の放電極と反対極に通電
されて成るため、効果的な塵埃等の捕集が可能で
ある。
In addition, since the collector constituting the cooling collection section has a honeycomb core body disposed on the lower surface of a perforated plate, dust and the like come into contact with and are collected by the liquid film flowing down the inner wall of the cell of the honeycomb core body. By configuring the charging section with a discharge counter electrode with multiple through holes and a discharge electrode with multiple pointed discharge needles located at the center of each through hole, the charging efficiency of dust, etc. is increased. In addition, since the cooling collection section is energized to the opposite pole to the discharge electrode of the charging section, it is possible to effectively collect dust and the like.

上記気−液接触にて生成された微細液滴は微細
水滴除去部に移行された後捕集される。そして、
清浄化された空気は再熱手段により熱されて所定
の温度及び湿度に調整された後、室内に循環され
る。
The fine droplets generated by the above-mentioned gas-liquid contact are transferred to the fine water droplet removal section and then collected. and,
The purified air is heated by the reheating means, adjusted to a predetermined temperature and humidity, and then circulated indoors.

また、第2の発明においては、冷却水槽内に収
容される捕集塵埃中の有害細菌を含む水を殺菌手
段にて殺菌処理することができるため、再度冷水
供給部に循環に供することが可能となる。
In addition, in the second invention, since the water containing harmful bacteria contained in the collected dust stored in the cooling water tank can be sterilized by the sterilizing means, it is possible to circulate it again to the cold water supply section. becomes.

[実施例] 以下にこの発明の実施例を添附図面に基いて詳
細に説明する。
[Examples] Examples of the present invention will be described in detail below with reference to the accompanying drawings.

◎第1の発明 第1図は第1の発明の湿式空気清浄装置の概
略断面図が示されている。
◎First invention FIG. 1 shows a schematic cross-sectional view of a wet air cleaning device according to the first invention.

この発明の湿式空気清浄装置は、下部に温度
調整手段である冷却コイル16により温度調整
される水を収容する冷却水槽18を設け、か
つ、その上部側方に空気流入口12を開口する
と共に、上部に空気流出口14を開口する筒状
の空気清浄装置本体10と、空気清浄装置本体
10内の空気流入口12と空気流出口14の中
間部に下方向きに配設される冷水供給部20
と、冷水供給部20の下方上流側に水平状に配
設される冷却捕集部30と、冷水供給部20の
上方下流側に向つて順次配設される微細水滴除
去部40及び再熱手段である再熱コイル50と
で構成され、そして、空気流入口12の上流側
に荷電部60を設けると共に、送風手段である
送風フアン70を介して室72の吸込口71に
接続し、空気流出口14を室72の吹出口73
に接続して成る構造となつている。
The wet air purifying device of the present invention is provided with a cooling water tank 18 in the lower part of which contains water whose temperature is adjusted by a cooling coil 16 serving as a temperature adjustment means, and has an air inlet 12 opened on the side of the upper part. A cylindrical air purifier main body 10 having an air outlet 14 opened at the top, and a cold water supply section 20 disposed downwardly in the middle part between the air inlet 12 and the air outlet 14 in the air purifier main body 10.
, a cooling collection section 30 disposed horizontally on the lower upstream side of the cold water supply section 20 , a fine water droplet removing section 40 and a reheating means disposed in sequence toward the upper downstream side of the cold water supply section 20 A charging unit 60 is provided on the upstream side of the air inlet 12, and it is connected to the suction port 71 of the chamber 72 via a blower fan 70, which is a blower means, to control the air flow. The outlet 14 is connected to the air outlet 73 of the chamber 72.
It has a structure that is connected to.

上記冷却コイル16は冷却水槽18の上部に
配設されるか、あるいは、第1図に想像線で示
すように冷却水槽18内に配設される蛇行状の
蒸発器にて形成されており、また、上記再熱コ
イル50も冷却コイル16と同様に蛇行状の凝
縮器にて形成されており、そして、これら冷却
コイル16と再熱コイル50とは同一のヒート
ポンプ80をを介して接続されている。このヒ
ートポンプ80は圧縮機82、凝縮器50,8
4、レシーバタンク86、蒸発器16及びアキ
ユムレータ88等にて構成されている。なお、
再熱コイル50は、凝縮器を用いず、電気ヒー
タ50′や別個の加熱源(図示せず)につなが
る温水流通交換器とすることもできる。
The cooling coil 16 is disposed above the cooling water tank 18, or is formed by a meandering evaporator disposed within the cooling water tank 18 as shown in phantom lines in FIG. Further, the reheating coil 50 is also formed of a meandering condenser like the cooling coil 16, and the cooling coil 16 and the reheating coil 50 are connected via the same heat pump 80. There is. This heat pump 80 includes a compressor 82, condensers 50, 8
4, a receiver tank 86, an evaporator 16, an accumulator 88, etc. In addition,
The reheat coil 50 can also be a hot water flow exchanger without a condenser and connected to an electric heater 50' or a separate heating source (not shown).

上記冷水供給部20は、上記冷却水槽18に
循環ポンプ22を介して接続されて、冷却水槽
18内の水が循環供給されるようになつてい
る。この冷水供給部20は、第5図及び第6図
に示すように、冷却水槽18に接続する管路2
1から分岐された2つの分岐管路23にそれぞ
れ下向きに開口する噴管24の開口の下方に3
本の支持棒25,25,25にて支持される多
孔の拡散板26を有する散水器28にて構成さ
れている。この冷水供給部20から散布される
冷水は上記冷却コイル16にて冷却され、汚染
空気を露点以下に冷却でき、かつ、凍結しない
温度となつている。
The cold water supply unit 20 is connected to the cooling water tank 18 via a circulation pump 22, so that the water in the cooling water tank 18 is circulated and supplied. As shown in FIGS. 5 and 6, this cold water supply section 20 has a pipe line 2 connected to the cooling water tank 18.
3 below the opening of the jet pipe 24 which opens downward into two branch pipes 23 branched from 1.
It consists of a water sprinkler 28 having a porous diffusion plate 26 supported by book support rods 25, 25, 25. The cold water sprayed from the cold water supply section 20 is cooled by the cooling coil 16, and has a temperature that can cool the contaminated air below the dew point and does not freeze.

上記冷水供給部20の下方上流側に配設され
る冷却捕集部30は、第3図に示すように、多
孔板34と、それぞれの多孔板34の下面にハ
ニカムコア体32を配設した捕集体36を1組
又は複数組配設したものにて形成される。この
場合、捕集体36,36,36は互いに適宜間
隔をおいて空気清浄装置本体10内に水平状に
配設されており、また、ハニカムコア体32
は、一層のハニカムコア素材38でもよいが、
望ましくは第7図及び第8図に示すように、そ
の透孔33,33…同士が互いに偏倚する複数
(図面では2枚の場合を示す)のハニカムコア
素材38,38にて形成する方がよい。このよ
うに構成される冷却捕集部30は、荷電部60
にて帯電された塵埃を含む空気が通過する際、
荷電部60との電位差による静電誘導作用によ
つて塵埃を捕集するものであつて、荷電部60
の放電極68と反対極に導電されて成り、例え
ば、第3図に示すように、荷電部60の放電極
68に負極性の電圧を印加する電源61の陽極
側に接続することにより、効率良く塵埃の捕集
を行うようになつている。
As shown in FIG. 3, the cooling collection unit 30 disposed on the lower upstream side of the cold water supply unit 20 includes a perforated plate 34 and a honeycomb core body 32 disposed on the lower surface of each perforated plate 34. It is formed by arranging one or more sets of collectors 36. In this case, the collectors 36, 36, 36 are arranged horizontally in the air purifier main body 10 at appropriate intervals from each other, and the honeycomb core body 32
may be a single layer honeycomb core material 38, but
Preferably, as shown in FIGS. 7 and 8, the honeycomb core material 38, 38 is formed of a plurality of honeycomb core materials 38, 38 whose through holes 33, 33 are offset from each other (the drawing shows the case of two sheets). good. The cooling collection section 30 configured in this manner includes the charging section 60
When air containing charged dust passes through,
The device collects dust by an electrostatic induction effect caused by a potential difference between the charging section 60 and the charging section 60.
For example, as shown in FIG. 3, by connecting the discharge electrode 68 of the charging section 60 to the anode side of a power source 61 that applies a negative polarity voltage, the efficiency can be improved. It has become effective at collecting dust.

上記冷水供給部20の上方下流側に配設され
る微細水滴除去部40は、上記冷却捕集部30
を構成するハニカムコア体32と同様なハニカ
ムコア体42、このハニカムコア体32の上面
に接触配設される第1のミストリミネータ44
と、この第1のミストエリミネータ44の上方
下流側に適宜間隔をおいて配設される第2のミ
ストエリミネータ46とで構成されている。
The fine water droplet removal section 40 disposed above and downstream of the cold water supply section 20 is connected to the cooling collection section 30.
A honeycomb core body 42 similar to the honeycomb core body 32 constituting the honeycomb core body 32, and a first mist limitator 44 disposed in contact with the upper surface of the honeycomb core body 32.
and a second mist eliminator 46 disposed above and downstream of the first mist eliminator 44 at an appropriate interval.

一方、上記荷電部60は、第2図に示すよう
に、複数の透孔62,62…を穿設する放電対
極64と、この放電対極64の各透孔62の中
心に位置する複数の先尖状放電針66,66…
を突設する放電極68とで構成されている。荷
電部60をこのように構成することにより、空
気清浄装置本体10に送られた室内の汚染され
た空気は透孔62,62…によつて整流かつ分
散されて流速が均一になつて通過するので、各
透孔62の中心に突出する放電極68によつて
空気中の塵埃は確実に帯電され、帯電効率を高
くすることができ、その結果捕集効率を高める
ことができる。また、透孔62を有する放電対
極64に先尖状放電針66を突設する放電局6
8を対向配置すればよいので、放電対極64と
放電極68とを容易に位置決めでき、しかも、
構造が簡単であるので、製造コストを低減する
ことができる。なおこの場合、放電対極64は
アルミニウム合金等の金属板又は少なくとも透
孔62を含む表面に導電性金属を被覆した樹脂
基板にて形成される。また、上記放電極68は
例えば板厚が0.1〜0.3mm好ましくは0.2〜1.0mm
のステンレス鋼あるいは普通鋼、銅、真鍮、ア
ルミニウム等の強度を有する導電性金属板にて
形成されている。このように構成される荷電部
60において、放電極68が電源61の陰極
に、放電対極64が電源61の陽極に接続され
ており、これら放電極68と放電対極64に電
圧が印加されると、両者間においてコロナ放電
が生じるようになつている。なお、この場合、
放電極68と放電対極64とを逆極性にして正
極性放電を行うようにしてもよい。かかるコロ
ナ放電は一般の交流電源(100V〜200V)を変
圧し、かつ、整流することで得られる直流電圧
−4.5KV〜−5KV、一針当りの放電流2〜
20μAの直流電流で行うことができる。
Meanwhile, as shown in FIG. 2, the charging section 60 includes a discharge counter electrode 64 having a plurality of through holes 62, 62, . Pointed discharge needles 66, 66...
and a discharge electrode 68 protruding from the discharge electrode 68. By configuring the charging section 60 in this way, the indoor contaminated air sent to the air purifier main body 10 is rectified and dispersed by the through holes 62, 62..., and passes through with a uniform flow velocity. Therefore, the dust in the air is reliably charged by the discharge electrode 68 protruding from the center of each through hole 62, and the charging efficiency can be increased, and as a result, the collection efficiency can be increased. Further, a discharge station 6 in which a pointed discharge needle 66 is protruded from a discharge counter electrode 64 having a through hole 62 is provided.
Since it is only necessary to arrange the electrodes 8 facing each other, the discharge counter electrode 64 and the discharge electrode 68 can be easily positioned.
Since the structure is simple, manufacturing costs can be reduced. In this case, the discharge counter electrode 64 is formed of a metal plate such as an aluminum alloy or a resin substrate whose surface including at least the through holes 62 is coated with a conductive metal. Further, the discharge electrode 68 has a plate thickness of, for example, 0.1 to 0.3 mm, preferably 0.2 to 1.0 mm.
It is made of a strong conductive metal plate such as stainless steel, ordinary steel, copper, brass, or aluminum. In the charging section 60 configured as described above, the discharge electrode 68 is connected to the cathode of the power source 61, and the discharge counter electrode 64 is connected to the anode of the power source 61. When a voltage is applied to the discharge electrode 68 and the discharge counter electrode 64, , a corona discharge is generated between the two. In this case,
The discharge electrode 68 and the discharge counter electrode 64 may have opposite polarities to perform positive discharge. Such corona discharge is obtained by transforming and rectifying a general AC power supply (100V to 200V), with a DC voltage of -4.5KV to -5KV, and a discharge current per stitch of 2 to 5KV.
This can be done with a direct current of 20 μA.

上記荷電部60にも冷水供給部20からの水
滴がかかるが、荷電部60を、第4A図及び第
4図Bに示すように、空気清浄装置本体10と
流入側管11とを接続する荷電部ダクト11a
内に配設される塩化ビニル製方形枠11bにて
放電対極64を絶縁状態に支持し、また、スペ
ーサ11c及び支持棒11dを介して適宜間隔
をおいて支持される放電対極68を方形枠11
bに架設して取付けることにより、シヨートを
防止することができる。しかも、この場合、印
加電圧が低電圧であるため、安全である。な
お、電源61へのリード線(図示せず)は水滴
のない上流側に配線する方がよい。なおこの場
合、放電極68と空気流入口12との距離1は
可及的に狭くすることが望ましい。その理由
は、帯電された塵埃粒子が冷却捕集部30に到
達する前に粒子間の放電やダクト内壁に付着す
るのを防止するためである。また、荷電部60
の別のシヨート防止構造としては、第4C図に
示すように、荷電部ダクト11aの上部壁にシ
リコンゴムあるいはフツ素ゴム等のシールパツ
キング11fを介して取付けられる碍子11g
にて放電対極64及び放電極68をそれぞれ吊
下げた状態で保持するものも考えられる。この
場合、硝子11gの周囲に乾燥用ヒータ11h
を配設して硝子11gの表面への結露による漏
電を防止するか、あるいは、乾燥空気吹付けノ
ズル(図示せず)を設けておく。なお、空気清
浄装置本体10の空気流入口側の上部に飛沫防
止用邪魔板11iを設けることにより、飛沫の
荷電部60への侵入を少なくすることができ
る。
Although water droplets from the cold water supply section 20 are applied to the charging section 60, the charging section 60 is connected to a charging section that connects the air purifier main body 10 and the inflow side pipe 11, as shown in FIGS. 4A and 4B. Part duct 11a
A discharge counter electrode 64 is supported in an insulated state by a rectangular frame 11b made of vinyl chloride disposed inside the rectangular frame 11, and a discharge counter electrode 68 supported at appropriate intervals via a spacer 11c and a support rod 11d is supported in a rectangular frame 11.
By constructing and attaching it to b, it is possible to prevent shoots. Moreover, in this case, since the applied voltage is low, it is safe. Note that it is better to wire the lead wire (not shown) to the power source 61 on the upstream side where there are no water droplets. In this case, it is desirable to make the distance 1 between the discharge electrode 68 and the air inlet 12 as narrow as possible. The reason for this is to prevent electrical discharge between particles and to prevent the charged dust particles from adhering to the inner wall of the duct before reaching the cooling collection section 30. In addition, the charging section 60
As another shot prevention structure, as shown in FIG. 4C, an insulator 11g is attached to the upper wall of the charging section duct 11a via a seal packing 11f made of silicone rubber or fluorine rubber.
It is also conceivable to hold the discharge counter electrode 64 and the discharge electrode 68 in a suspended state. In this case, a drying heater 11h is placed around the glass 11g.
is provided to prevent electrical leakage due to dew condensation on the surface of the glass 11g, or a dry air blowing nozzle (not shown) is provided. In addition, by providing the splash prevention baffle plate 11i on the upper part of the air inlet side of the air purifying device main body 10, it is possible to reduce the intrusion of droplets into the charging section 60.

また、上記空気清浄装置本体10の空気流入
口12と室72の吸込口71とを接続する流入
側管路11の送風フアン70の上流側には切換
弁74を介して外気導入管路13が接続されて
いる。
Further, an outside air introduction pipe 13 is connected via a switching valve 74 to the upstream side of the blower fan 70 of the inflow side pipe 11 that connects the air inlet 12 of the air purifier main body 10 and the suction port 71 of the chamber 72. It is connected.

なお、上記冷却水槽18と冷水供給部20と
を接続する循環管路21には流量計27が配設
されており、かつ、この循環管路21から分岐
された分岐管路23′には上記冷却捕集部30
の下方上流側に位置する補助冷水供給部20′
が接続されている。この補助冷水供給部20′
は、第9図ないし第11図に示すように、分岐
管路23′の先端にエルボ管29を介して下方
に開口すると噴管24と、この噴管24の開口
側に2本の支持棒25a,25aにて支持され
る円錐状拡散板26aとで構成されている。な
お、補助冷水供給部20′は必ずしも設ける必
要はない。
A flow meter 27 is disposed in the circulation pipe 21 connecting the cooling water tank 18 and the cold water supply section 20, and a branch pipe 23' branched from the circulation pipe 21 has the above-mentioned Cooling collection section 30
Auxiliary cold water supply section 20' located on the lower upstream side of
is connected. This auxiliary cold water supply section 20'
As shown in FIGS. 9 to 11, when the branch pipe 23' opens downward through an elbow pipe 29, there is a jet pipe 24 and two support rods on the opening side of the jet pipe 24. 25a, and a conical diffusion plate 26a supported by 25a. Note that the auxiliary cold water supply section 20' does not necessarily need to be provided.

また、上記空気清浄装置本体10の空気流入
口12、冷水供給部20付近及び空気流出口側
の微細水滴除去部40の上方下流側にはそれぞ
れ温度・湿度センサ51,52,53が配置さ
れており、これらセンサ51,52,53から
の検知信号を受ける制御装置(図示せず)から
上記ヒートポンプ80,循環ポンプ22等に制
御指令が送られるようになつている。
Further, temperature/humidity sensors 51, 52, and 53 are arranged near the air inlet 12 and the cold water supply section 20 of the air purifier main body 10, and on the upper and downstream side of the fine water droplet removing section 40 on the air outlet side, respectively. Control commands are sent to the heat pump 80, circulation pump 22, etc. from a control device (not shown) that receives detection signals from these sensors 51, 52, and 53.

上記のように構成されるこの発明の空気清浄
装置において、送風フアン70が駆動され、室
内の汚染された空気が空気清浄装置本体10内
に送込まれると、空気中の塵埃等はまず荷電部
60により帯電された後、空気流入口12から
空気清浄装置本体10内の冷却捕集部30を通
過する。このとき、空気中の塵埃の一部は冷却
捕集部30のハニカムコア体32の透孔33を
通過する際に捕集され、ハニカムコア体32を
通過した空気は多孔板34の目孔35,35…
を通過するが、この際、冷水供給部20から散
布されて多孔板34上に形成された液膜を激し
く破りながら微細な液滴と微細な気泡を生成す
る。その結果、第4図に示すように、多孔板3
4上には粉体の流動層に酷似した濃密な液滴流
動域37が空気圧損と均衡して適当な厚みで形
成される。この液滴流動域37は汚染空気の流
速が増すに従つてその厚みを増す。汚染空気中
の塵埃は、多孔板34の目孔35,35…に張
られた滴膜を破るとき、及び多孔板34上に形
成された液滴流動域37を通過する際に、塵埃
粒子の液滴への慣性衝突作用、拡散作用、凝集
作用及び静電誘導作用によつて効果的に気液接
触が行われ、塵埃は十分液側に移行する。
In the air purifier of the present invention configured as described above, when the blower fan 70 is driven and indoor contaminated air is sent into the air purifier main body 10, the dust and the like in the air is first transferred to the charged section. After being charged by 60, the air passes through the cooling collection section 30 in the air purifier main body 10 from the air inlet 12. At this time, part of the dust in the air is collected when passing through the holes 33 of the honeycomb core body 32 of the cooling collection unit 30, and the air that has passed through the honeycomb core body 32 is collected through the holes 33 of the porous plate 34. ,35...
At this time, the liquid is sprayed from the cold water supply section 20 and violently breaks the liquid film formed on the perforated plate 34, generating fine droplets and fine bubbles. As a result, as shown in FIG.
4, a dense droplet flow region 37 that closely resembles a fluidized bed of powder is formed with an appropriate thickness in balance with the air pressure loss. This droplet flow region 37 increases in thickness as the flow rate of contaminated air increases. Dust in contaminated air breaks down into dust particles when it breaks through the droplet film stretched over the holes 35, 35... of the perforated plate 34, and when it passes through the droplet flow area 37 formed on the perforated plate 34. Gas-liquid contact is effectively carried out by the inertial collision effect, diffusion effect, agglomeration effect, and electrostatic induction effect on the droplets, and dust is sufficiently transferred to the liquid side.

汚染空気が上記捕集体36の多孔板34上で
跳上げた液滴のうち細かい液滴は上方の捕集体
36のハニカムコア素材38に運ばれてハニカ
ムコア素材38の透孔33の内壁を濡らしなが
ら下降し、大きな液滴となつて再び下段の多孔
板34上に戻る。従つて、汚染空気中の塵埃
は、ハニカムコア素材38の透孔33内壁でも
上記物理的、静電誘導的接触が行われて除去さ
れ、清浄化され、従来の湿式集塵方式では困難
とされていた0.5〜0.1μmの微細塵埃を捕集す
ることができる。そして、清浄化された空気は
再熱コイル50にて所定の温度(約25℃)に加
熱され及び調湿された後、室72の吸込口71
に送られる。
Among the droplets that the contaminated air jumps up on the perforated plate 34 of the collector 36, fine droplets are carried to the honeycomb core material 38 of the collector 36 above and wet the inner walls of the through holes 33 of the honeycomb core material 38. The droplet then returns to the lower perforated plate 34 again as a large droplet. Therefore, the dust in the contaminated air is removed and purified by the above-mentioned physical and electrostatic induction contact even on the inner wall of the through hole 33 of the honeycomb core material 38, which is difficult to do with the conventional wet dust collection method. It can collect fine dust of 0.5 to 0.1 μm. Then, the purified air is heated to a predetermined temperature (approximately 25° C.) and humidity controlled by the reheating coil 50, and then
sent to.

次に、上記のように構成されるこの発明の空
気清浄装置を夏期及び冬期の下で使用した場合
の具体例を第12図及び第13図の空気線図を
参照して説明する。すなわち、夏期の場合(第
12図)は室72からの空気は外気と混合
(混合点の温度:T3)した後、空気清浄装
置本体10内に送られて冷水供給部20からの
冷水によつて冷却され、第2のミストエリミネ
ータ46の出口付近の温度がT4に冷却され、
かかる低温飽和空気を室72の吹出温T2に上
げるため、再熱コイル50によつて加熱(加
熱後の温度:T5)された後、室72内に供給
される。このようにして室72内に供給される
清浄化空気は熱負荷も加わり適湿(T2)及び
適温(40〜60%)とすることができる。
Next, a specific example of the use of the air purifying apparatus of the present invention constructed as described above in summer and winter will be described with reference to the psychrometric diagrams of FIGS. 12 and 13. That is, in the summer (FIG. 12), the air from the chamber 72 is mixed with outside air (temperature at the mixing point: T 3 ), and then sent into the air purifier main body 10 and mixed with cold water from the cold water supply section 20. As a result, the temperature near the outlet of the second mist eliminator 46 is cooled to T4 ,
The low-temperature saturated air is heated by the reheating coil 50 (temperature after heating: T 5 ) in order to raise the blowing temperature of the chamber 72 to T 2 and then supplied into the chamber 72 . The clean air supplied into the chamber 72 in this manner can be kept at an appropriate humidity (T 2 ) and an appropriate temperature (40 to 60%) due to the addition of a thermal load.

なお、冬期の場合(第13図)は、室72か
らの空気は外気と混合(混合点、混合点
の温度:T3とする)した後、空気清浄装置本
体10内に送られて、冷水供給部20からの温
水(冬期は冷水相当部分の水をヒートポンプ8
0によつて冷却コイル16を凝縮器として働か
せて加温する。)によつて加湿され、第2のミ
ストエリミネータ46の出口付近の湿度が飽
和点近くまで加湿され(RH95〜100%)、ヒー
トポンプ80とは別に放置された加熱ヒータ
(例えば伝熱ヒータ、温水ヒータ、蒸気ヒータ
等)50′で室72への吹出温度まで再熱さ
れる。このようにして室72内に供給される清
浄化空気は適温(T2)及び適湿(RH40〜60
%)とすることができる。
In addition, in the case of winter (Fig. 13), the air from the room 72 is mixed with outside air (mixing point, temperature at the mixing point: T 3 ), and then sent into the air purifier main body 10 and cooled water. The hot water from the supply section 20 (in winter, the portion equivalent to cold water) is supplied to the heat pump 8.
0 causes the cooling coil 16 to function as a condenser and heat it. ), the humidity near the outlet of the second mist eliminator 46 is humidified to near the saturation point (RH95-100%), and a heater (e.g., a heat transfer heater, a hot water heater) left separately from the heat pump 80 is used. , steam heater, etc.) 50' to the temperature at which it is blown into the chamber 72. The purified air thus supplied into the room 72 has an appropriate temperature ( T2 ) and appropriate humidity (RH40~60).
%).

◎第2の発明 第14図は第2の発明に係る空気清浄装置の
第一実施例を示す概略断面図で、この発明の空
気清浄装置は、上記第1の発明の空気清浄装置
の冷却水槽内の冷水を殺菌処理すべく冷却水槽
に殺菌処理手段を接続した場合である。すなわ
ち、上記循環管路21の上流側に接続する第1
の管路91を介して殺菌処理手段であるオゾン
殺菌槽90の供給側を接続すると共に、オゾン
殺菌槽90の吐出側を第2の管路92を介して
循環管路21の下流側に接続し、そして、オゾ
ン殺菌槽90内に配設されたオゾン曝気部93
にオゾン発生器94を接続した場合である。こ
の場合、オゾン発生器94は高電圧手段94a
を利用した放電作用によつてオゾンを生成する
ようになつている。
◎Second Invention Fig. 14 is a schematic sectional view showing a first embodiment of an air purifying device according to the second invention, and the air purifying device of this invention has a cooling water tank of the air purifying device of the first invention. This is a case where a sterilizing means is connected to the cooling water tank to sterilize the cold water inside. That is, the first
The supply side of an ozone sterilization tank 90, which is a sterilization treatment means, is connected through a pipe 91, and the discharge side of the ozone sterilization tank 90 is connected to the downstream side of the circulation pipe 21 via a second pipe 92. and an ozone aeration section 93 disposed within the ozone sterilization tank 90.
This is the case when an ozone generator 94 is connected to the In this case, the ozone generator 94 is a high voltage means 94a.
Ozone is now produced by the discharge action using

なお、第2の発明において、その他の部分は
上記第1の発明と同一であるので、同一の構成
部分には同一符号を付してその説明は省略す
る。
Note that in the second invention, other parts are the same as those in the first invention, so the same components are given the same reference numerals and the explanation thereof will be omitted.

上記のように構成することにより、冷却水槽
18からオゾン殺菌槽90内に供給された冷水
はオゾン発生器94からオゾン曝気部93に供
給されて散気されるオゾンによつて殺菌され
る。そして、殺菌された冷水は循環管路21を
介して冷水供給部20から汚染空気に散布され
るのである。
With the above configuration, the cold water supplied from the cooling water tank 18 into the ozone sterilization tank 90 is sterilized by the ozone supplied from the ozone generator 94 to the ozone aeration section 93 and diffused. The sterilized cold water is then sprayed into the contaminated air from the cold water supply section 20 via the circulation pipe 21.

第15図は第2の発明の第二実施例を示す概
略断面図で、上記冷却水槽18と殺菌処理手段
とを兼用させた場合である。すなわち、空気清
浄装置本体10の下部に循環切換弁21aを介
して2つの冷却兼オゾン殺菌水槽18a,18
bを配設し、各冷却兼オゾン殺菌水槽18a,
18b内にオゾン曝気部93を配設すると共
に、オゾン切換弁95を介してオゾン発生器9
4を接続した場合である。また、これら冷却兼
オゾン殺菌水槽18a,18bにはオゾン排出
切換弁96を介して電気ヒータ97aを具備す
るオゾン分解器97が接続されている。なお、
冷却兼オゾン殺菌水槽18a,18b内には必
要に応じて冷却あるいは加熱する冷却兼加熱コ
イル16a,16bが配設されるととに、水槽
18a,18b内の冷水を撹拌する撹拌器9
8,98が配設されている。また、オゾン発生
器94は空気流路99を介して上記空気清浄装
置本体10の空気流出口14側の清浄空気が供
給されるようになつている。
FIG. 15 is a schematic sectional view showing a second embodiment of the second invention, in which the cooling water tank 18 is used also as a sterilizing means. That is, two cooling/ozone sterilization water tanks 18a, 18 are connected to the lower part of the air purifier main body 10 via the circulation switching valve 21a.
b, each cooling and ozone sterilization water tank 18a,
An ozone aeration section 93 is provided in the ozone generator 9 through the ozone switching valve 95.
This is the case when 4 is connected. Further, an ozone decomposer 97 equipped with an electric heater 97a is connected to these cooling and ozone sterilization water tanks 18a and 18b via an ozone discharge switching valve 96. In addition,
In the cooling/ozone sterilization water tanks 18a, 18b, cooling/heating coils 16a, 16b are provided to cool or heat the water as needed, and a stirrer 9 is provided to stir the cold water in the water tanks 18a, 18b.
8,98 are arranged. Further, the ozone generator 94 is supplied with clean air from the air outlet 14 side of the air purifier main body 10 through an air flow path 99.

上記のように構成される空気清浄装置によれ
ば、循環切換弁21aを切換えて一方の冷却兼
オゾン殺菌水槽18aを空気清浄装置本体10
に接続し、他方の冷却オゾン殺菌水槽18bを
空気清浄装置本体10から遮断することができ
るので、連続して空気清浄と冷水の殺菌処理を
行うことができ、過剰オゾンはオゾン分解器9
7にて完全分解して外気中に排気することがで
きる。この場合、オゾン発生器94からのオゾ
ンを冷却兼オゾン殺菌水槽18b中の冷水に曝
気し、水中オゾン濃度を0.5ppmとし、オゾン
分解器97の加熱温度を約400℃とすると、オ
ゾン濃度0.5ppmで約30分で殺菌できるが、殺
菌後約10時間放置しておく、なおこの場合、冷
却兼オゾン殺菌水槽18b内を冷却兼加熱コイ
ル16aにて30〜40℃に加熱しておけばオゾン
分解時間を短縮することができる。また、冷水
を加熱した場合には、冷水供給部20に循環さ
せる際に冷却兼加熱コイル16aにて所定温度
まで冷却する。このとき、オゾン発生器94は
停止させておくことは勿論である。
According to the air purifying device configured as described above, the circulation switching valve 21a is switched to connect one of the cooling and ozone sterilizing water tanks 18a to the air purifying device main body 10.
Since the other cooling ozone sterilization water tank 18b can be isolated from the air purifier main body 10, air purification and cold water sterilization can be performed continuously, and excess ozone can be removed from the ozone decomposer 9.
7, it can be completely disassembled and exhausted to the outside air. In this case, if the ozone from the ozone generator 94 is aerated to the cold water in the cooling/ozone sterilization water tank 18b, and the ozone concentration in the water is 0.5 ppm, and the heating temperature of the ozone decomposer 97 is approximately 400°C, the ozone concentration is 0.5 ppm. It can be sterilized in about 30 minutes, but leave it for about 10 hours after sterilization. In this case, ozone decomposition can be done by heating the inside of the cooling/ozone sterilization water tank 18b to 30 to 40°C with the cooling/heating coil 16a. It can save time. Further, when the cold water is heated, it is cooled to a predetermined temperature by the cooling/heating coil 16a when circulating to the cold water supply section 20. At this time, of course, the ozone generator 94 is stopped.

第16図は上記冷却兼加熱コイル16aの加
熱手段のかわりに紫外線燈を使用した場合であ
る。すなわち、冷却兼オゾン殺菌水槽18a,
18b内に4つの紫外線燈16b,16b…を
配設することにより加熱コイルを省略した場合
である。なおこの場合は冷却コイル16は水槽
18a,18bの上部に配設するか、あるい
は、水槽18a,18b内に配設させておく必
要がある。
FIG. 16 shows a case where an ultraviolet lamp is used instead of the heating means of the cooling/heating coil 16a. That is, the cooling and ozone sterilization water tank 18a,
This is a case in which the heating coil is omitted by arranging four ultraviolet lamps 16b, 16b, . . . in 18b. In this case, the cooling coil 16 must be placed above the water tanks 18a, 18b, or within the water tanks 18a, 18b.

第17図ないし第19図は第2の発明の第三
実施例を示す概略断面図及びその要部拡大断面
図を示すもので、冷却水槽内の冷水を光化学反
応によるオゾン発生器によつて殺菌処理を行う
ようにした場合である。すなわち、上記冷却水
槽18の底部を仕切り板101にて一部が連通
するように区画し、区画された水槽下部100
内に千鳥状に配設される複数の酸化チタン製の
被照射体110,110…と、被照射体11
0,110…のそれぞれ隣接する被照射体11
0,110間に配設される発光体120,12
0…とでオゾン発生器94を形成して、冷却水
槽18内に収容される冷水を水槽下部100内
に供給しつつ迂回させながら光化学反応で生成
されたオゾンにより殺菌させるようにした場合
である。この場合、被照射体110は、酸化チ
タン(TiO2)をアセチレンロースフイルムに
固着させたフイルム112を透明アクリル板あ
るいはステンレス板等の板材114に貼着して
成り、ブラケツト116をもつて水槽下部10
0内に固定されるようになつている(第19図
参照)。また、発光体120は、水銀燈あるい
は紫外線燈等の光源122を石英管124内に
配置した構造であつて、水槽下部100に固定
される支持部材126にて固定保持されるよう
になつている(第19図参照)。
Figures 17 to 19 are schematic cross-sectional views and enlarged cross-sectional views of essential parts of a third embodiment of the second invention, in which cold water in a cooling water tank is sterilized by an ozone generator using a photochemical reaction. This is a case where processing is performed. That is, the bottom of the cooling water tank 18 is partitioned by the partition plate 101 so that a part thereof is communicated with the partitioned water tank lower part 100.
A plurality of titanium oxide irradiated objects 110, 110... arranged in a staggered manner inside the irradiated object 11
0,110...respectively adjacent irradiated objects 11
Light emitters 120 and 12 arranged between 0 and 110
This is a case in which an ozone generator 94 is formed with 0..., and the cold water contained in the cooling water tank 18 is supplied into the lower part 100 of the water tank and detoured while being sterilized by ozone generated by a photochemical reaction. . In this case, the irradiated object 110 is made by pasting a film 112 in which titanium oxide (T i O 2 ) is fixed to an acetylene film on a plate material 114 such as a transparent acrylic plate or a stainless steel plate, and is attached with a bracket 116 . Water tank lower part 10
It is designed to be fixed within 0 (see FIG. 19). Further, the light emitting body 120 has a structure in which a light source 122 such as a mercury lamp or an ultraviolet lamp is disposed inside a quartz tube 124, and is fixedly held by a support member 126 fixed to the lower part 100 of the aquarium ( (See Figure 19).

第20図及び第21図は第2の発明の第三実
施例の別の形態を示す断面図及びその要部斜視
図で、被照射体の照射位置を移動変換可能にし
た場合である。すなわち、冷却水槽18内に互
いに間隔をおいて配設される複数の被照射体1
10,110…の各々を一対のローラ132,
134間に掛渡されるベルト体130にて形成
し、一方のローラ132を冷却水槽18の外に
配設される駆動モータ136によつて駆動させ
るようにした場合である。この場合、ベルト体
130は、上記被照射体110と同様に、酸化
チタン(TiO2)をアセチレンロースフイルム
に固着させたフイルム112をベルト基材に貼
着した構造となつており、固定バンド等の固定
手段131にて無端状に形成されている。ま
た、隣接するベルト体130は互いに反対方向
に回転し得るように駆動モータ136の駆動プ
ーリ136aと駆動ローラ132,132…の
プーリ132a,132a…とは、たすき掛け
になつている。
FIGS. 20 and 21 are a cross-sectional view and a perspective view of a main part of another embodiment of the third embodiment of the second invention, in which the irradiation position of the object to be irradiated can be moved and changed. That is, a plurality of irradiated objects 1 are arranged at intervals in the cooling water tank 18.
10, 110... are each connected to a pair of rollers 132,
134, and one roller 132 is driven by a drive motor 136 disposed outside the cooling water tank 18. In this case, the belt body 130 has a structure in which a film 112 in which titanium oxide (T i O 2 ) is fixed to an acetylene loin film is adhered to a belt base material, similar to the irradiated body 110 described above. It is formed into an endless shape by a fixing means 131 such as a band. Further, the drive pulley 136a of the drive motor 136 and the pulleys 132a, 132a, .

上記のようにオゾン発生器を酸化チタン製被
照射体110と発光体120とで構成すことに
より、酸化チタン2TiO2に光を照射すると、光
化学反応によつて、TiO2+(O)となり、この際
生成されたオゾン(O)によつて冷水の殺菌処理が
行われる。
By configuring the ozone generator with the titanium oxide irradiated body 110 and the light emitting body 120 as described above, when titanium oxide 2TiO 2 is irradiated with light, it becomes TiO 2 +(O) through a photochemical reaction. The ozone (O) generated at this time sterilizes the cold water.

これは、例えば酸化チタン(TiO2)の存在
の下で光を照射すると、以下の酸化反応を行な
うことが周知であることからも類推できる。
This can be inferred from the fact that, for example, it is well known that when light is irradiated in the presence of titanium oxide (TiO 2 ), the following oxidation reaction occurs.

Hg→HgO CN-→CNO- なお、上記第三実施例において、冷却水槽1
8内の過剰オゾンを除去する場合には、上記第
一実施例及び第二実施例と同様にオゾン分解器
(図示せず)を設ける必要がある。
Hg→HgO CN - →CNO -In addition, in the third embodiment above, cooling water tank 1
In order to remove excess ozone in the 8, it is necessary to provide an ozone decomposer (not shown) as in the first and second embodiments.

第22図は、第2の発明の第四実施例を示す
もので、汚水を連続的に殺菌処理するようにし
た場合である。すなわち、第1の管路91、第
2の管路92と接続するオゾン殺菌槽90内に
紫外線殺菌装置94′を配設して、第1の管路
91からオゾン殺菌槽90内に流入する汚水を
紫外線殺菌装置94′にて殺菌処理した後、第
2の管路92から冷水供給部20へ連続的に送
水して、空気清浄化水として使用できるように
した場合である。
FIG. 22 shows a fourth embodiment of the second invention, in which wastewater is continuously sterilized. That is, an ultraviolet sterilizer 94' is disposed in the ozone sterilization tank 90 connected to the first pipe line 91 and the second pipe line 92, and the ultraviolet ray sterilizer 94' flows into the ozone sterilization tank 90 from the first pipe line 91. This is a case where the waste water is sterilized by the ultraviolet sterilizer 94' and then continuously fed to the cold water supply section 20 from the second pipe line 92 so that it can be used as air purifying water.

この汚水を連続的に殺菌処理をする手段は、
上記第三実施例の場合にも適用できる。すなわ
ち、第22A図に示すように、冷却水槽18の
下部100内を仕切り板101′,101′にて
千鳥状の迂回部100′,100′,100′を
形成すると共に、各迂回部100′内に紫外線
装置94′(紫外線灯)を配設することにより、
冷却水槽18の下部100内に収容された汚水
を、紫外線灯94′によつて連続的に殺菌処理
した後、循環ポンプ22によつて冷水供給部2
0へ送ることができる。
The means to continuously sterilize this wastewater is
This can also be applied to the case of the third embodiment. That is, as shown in FIG. 22A, staggered detour parts 100', 100', 100' are formed in the lower part 100 of the cooling water tank 18 by partition plates 101', 101', and each detour part 100' By installing an ultraviolet light device 94' (ultraviolet light) inside,
After the wastewater contained in the lower part 100 of the cooling water tank 18 is continuously sterilized by the ultraviolet lamp 94', it is transferred to the cold water supply section 2 by the circulation pump 22.
It can be sent to 0.

[発明の効果] 以上に説明したように、この発明の空気清浄装
置によれば、清浄及び調温・調湿化されるべき空
気中の塵埃、細菌等を荷電させる荷電部と、空気
に冷水微細ミストを接触する冷水供給部と、冷却
された塵埃等を捕集する冷却捕集部及び微細水滴
除去部と、清浄化された空気を調温・調湿するた
めの再熱手段を一箇所に集合すると共に、冷却捕
集部の捕集体を多孔板とこの多孔板の下面に配設
されるハニカムコア体とで構成し、荷電部を透孔
を穿設する放電対極と各透孔の中心に位置する先
尖状放電針とで構成し、かつ、冷却捕集部を荷電
部の放電極と反対極に通電するようにしたため、
以下のような効果が得られる。
[Effects of the Invention] As explained above, the air purifying device of the present invention includes a charging unit that charges dust, bacteria, etc. in the air to be cleaned, temperature controlled, and humidity controlled, and a charging unit that charges the air with cold water. A cold water supply unit that contacts fine mist, a cooling collection unit and a fine water droplet removal unit that collect cooled dust, and a reheating unit that controls the temperature and humidity of the purified air. The collecting body of the cooling collecting part is composed of a perforated plate and a honeycomb core body arranged on the lower surface of this perforated plate, and the charging part is composed of a discharge counter electrode with through holes and a discharge counter electrode with perforated holes. It consists of a pointed discharge needle located at the center, and the cooling collection part is energized to the opposite pole to the discharge electrode of the charging part.
The following effects can be obtained.

(1) 空気清浄機器、加熱部等の各機器を一箇所に
集中するので、スペースの有効利用が図れると
共に、メンテナンスの容易化が図れる。
(1) Since the air cleaning equipment, heating unit, and other equipment are concentrated in one place, space can be used effectively and maintenance can be facilitated.

(2) 集塵、調温・調湿等を1つの装置で行うの
で、コストの低廉化が図れ、併せて脱臭、殺菌
も容易に行える。
(2) Since dust collection, temperature control, humidity control, etc. are performed in one device, costs can be reduced, and deodorization and sterilization can also be easily performed.

(3) 汚染空気中の塵埃と液滴、液膜との間のクー
ロン力と、慣性衝突作用、拡散作用及び凝縮作
用によつて空気中の塵埃を捕集することができ
るため、従来の湿式集塵方式では困難とされて
いた微細粒子の塵埃を効率良く捕集することが
できる。
(3) Dust in the air can be collected by the Coulomb force between dust in contaminated air, droplets, and liquid film, as well as inertial collision, diffusion, and condensation effects, making it possible to collect dust in the air using the conventional wet method. It is possible to efficiently collect fine particles of dust, which is difficult to do with dust collection methods.

(4) 空気中の塵埃を帯電し、冷却捕集部及び微細
水滴除去部にて捕集するので、通常のフイルタ
のような目詰りによる風量の低下の虞れがな
く、また、集積塵埃(細菌を含む)の再飛散の
虞れもない。
(4) Since the dust in the air is charged and collected in the cooling collection section and the fine water droplet removal section, there is no risk of a reduction in air volume due to clogging, as is the case with ordinary filters, and the accumulated dust ( There is no risk of re-dispersal of bacteria (including bacteria).

(5) 冷却捕集部が、多孔板と、この多孔板の下面
に配設されるハニカムコア体とで構成される捕
集体であるので、ハニカムコア体のセル内壁を
流下する液膜に塵埃等を効率よく接触捕集する
ことができ、捕集効果を高めることができる。
(5) Since the cooling collection unit is a collection body composed of a perforated plate and a honeycomb core body disposed on the lower surface of the perforated plate, dust is not absorbed into the liquid film flowing down the inner wall of the cell of the honeycomb core body. etc. can be efficiently collected by contact, and the collection effect can be enhanced.

(6) 複数の透孔を穿設する放電対極と、各透孔の
中心に位置する複数の先尖状放電針を突設する
放電極とで荷電部を構成するので、空気清浄装
置本体に送られた室内の汚染された空気は透孔
によつて整流かつ分散されて流速が均一になつ
て通過するので、各透孔の中心に突出する放電
極によつて空気中の塵埃は確実に帯電され、帯
電効率を高くすることができ、その結果捕集効
率を高めることができる。また、放電対極と放
電極との位置決めが容易であり、構造も簡単で
ある。
(6) Since the charging part is composed of a discharge counter electrode with a plurality of through holes and a discharge electrode with a plurality of pointed discharge needles located at the center of each through hole, it is possible to The contaminated air sent into the room is rectified and dispersed by the through holes, and passes through with a uniform flow velocity.The discharge electrode protruding from the center of each through hole ensures that dust in the air is removed. It is electrically charged, and the charging efficiency can be increased, and as a result, the collection efficiency can be increased. Further, positioning of the discharge counter electrode and the discharge electrode is easy, and the structure is simple.

(7) 冷却捕集部を帯電した塵埃と反対極に通電す
るので、冷却捕集部における塵埃等の補集効率
が高い。
(7) Since the cooling collection section is energized to the opposite polarity to the charged dust, the efficiency of collecting dust, etc. in the cooling collection section is high.

(8) 交換や消耗部品がないので、長期間にわたつ
て連続運転が可能となる。
(8) Since there are no replacement or consumable parts, continuous operation is possible over a long period of time.

(9) 捕集された塵埃の細菌の増殖を防止すること
ができるので、冷却捕集部は衛生的である。
(9) The cooling collection section is sanitary because the growth of bacteria in the collected dust can be prevented.

(10) 再熱手段により冷却清浄下された湿式空気を
加熱するので、ミストの発生がない。
(10) Since the cooled and purified wet air is heated by the reheating means, no mist is generated.

また、第2の発明によれば、更に冷水供給部に
供給される冷却水を殺菌処理する手段を付加する
ため、上記(1)〜(10)に加えて殺菌のためのガスや薬
剤等を使用する必要がなく、これら殺菌用ガス等
によつて装置内部が腐蝕する虞れがない。しか
も、冷水は浄化されて、装置本体の冷水供給部へ
送給されるので、空気を確実に清浄化でき、二次
汚染心配もなく、衛生的である。
Further, according to the second invention, in order to further add means for sterilizing the cooling water supplied to the cold water supply section, in addition to the above (1) to (10), gas, chemicals, etc. for sterilization are added. There is no need to use it, and there is no risk that the inside of the device will be corroded by these sterilizing gases. Moreover, since the cold water is purified and sent to the cold water supply section of the main body of the apparatus, the air can be reliably purified, there is no risk of secondary contamination, and the apparatus is sanitary.

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

第1図はこの発明における第1の発明の空気清
浄装置を示す概略断面図、第2図はこの発明にお
ける荷電部の断面斜視図、第3図はこの発明にお
ける荷電部及び冷却捕集部の断面図、第4図はこ
の発明における冷却捕集部の作用状態を示す断面
図、第4A図はこの発明にける荷電部示す正面
図、第4B図はその側断面図、第4C図は荷電部
の別の構造を示す側断面図、第5図はこの発明に
おける冷水供給部の平面図、第6図はその側面
図、第7図はこの発明における微細水滴除去部の
要部平面図、第8図はその一部を断面で示す側面
図、第9図はこの発明における補助冷水供給部の
平面図、第10図及び第11図はそれぞれ第9図
の側面図及び要部拡大図、第12図及び第13図
はこの発明の空気清浄装置を稼働した場合の夏期
及び冬期の状態を示す空気線図、第14図はこの
発明の第2の発明の空気清浄装置の第一実施例を
示す概略断面図、第15図は第2の発明の第二実
施例を示す概略断面図、第16図は第三実施例の
別の形態を示す要部断面図、第17図は第2の発
明の第三実施例を示す概略断面図、第18図及び
第19図はそれぞれ第三実施例の要部断面図及び
その要部拡大図、第20図は第三実施例のに別の
形態を示す断面図、第21図はその要部である被
照射体の斜視図、第22図は第2の発明の第四実
施例を示す概略断面図、第22A図は第四実施例
の別の形態を示す概略断面図、第23図及び第2
4図は従来の湿式空気清浄装置の別の構造を示す
概略断面図である。 符号説明、10……空気清浄装置本体、12…
…空気流入口、14……空気流出口、16……冷
却コイル(温度調整手段)、16a……冷却兼加
熱コイル(温度調整手段)16b……紫外線燈、
18……冷却水槽、18a,18b……冷却兼オ
ゾン殺菌水槽、20……冷水供給部、30……冷
水捕集部、32……ハニカムコア体、34……多
孔板、36……捕集体、38……ハニカムコア素
材、40……微細水滴除去部、50……再熱コイ
ル(再熱手段)、60……荷電部、62……透孔、
64……放電対極、66……先尖状放電針、68
……放電極、70……送風フアン(送風手段)、
90……オゾン殺菌槽(殺菌手段)、93……オ
ゾン曝気部、94……オゾン発生部、94′……
紫外線殺菌装置、110……被照射体、120…
…発光体。
FIG. 1 is a schematic cross-sectional view showing an air purifying device according to a first aspect of the present invention, FIG. 2 is a cross-sectional perspective view of a charging section in this invention, and FIG. 3 is a schematic cross-sectional view showing a charging section and a cooling collection section in this invention. 4 is a sectional view showing the operating state of the cooling collection section in this invention, FIG. 4A is a front view showing the charging section in this invention, FIG. 4B is a side sectional view thereof, and FIG. 4C is a charging section. 5 is a plan view of the cold water supply section in the present invention, FIG. 6 is a side view thereof, and FIG. 7 is a plan view of essential parts of the fine water droplet removal section in the present invention. FIG. 8 is a side view showing a part of it in cross section, FIG. 9 is a plan view of the auxiliary cold water supply section in this invention, FIGS. 10 and 11 are a side view and an enlarged view of the main part of FIG. 9, respectively. Figs. 12 and 13 are psychrometric diagrams showing the conditions in summer and winter when the air purifying device of this invention is operated, and Fig. 14 is a first embodiment of the air purifying device of the second invention of this invention. 15 is a schematic sectional view showing a second embodiment of the second invention, FIG. 16 is a sectional view of main parts showing another form of the third embodiment, and FIG. 17 is a schematic sectional view showing a second embodiment of the second invention. FIG. 18 and FIG. 19 are a schematic cross-sectional view showing a third embodiment of the invention, respectively. FIG. 18 and FIG. 21 is a perspective view of the irradiated object which is the main part thereof, FIG. 22 is a schematic sectional view showing the fourth embodiment of the second invention, and FIG. 22A is a diagram of the fourth embodiment. Schematic sectional view showing another form, Fig. 23 and Fig. 2
FIG. 4 is a schematic sectional view showing another structure of a conventional wet air cleaning device. Explanation of symbols, 10... Air purifier main body, 12...
...Air inlet, 14...Air outlet, 16...Cooling coil (temperature adjustment means), 16a...Cooling/heating coil (temperature adjustment means) 16b...Ultraviolet lamp,
18... Cooling water tank, 18a, 18b... Cooling and ozone sterilization water tank, 20... Cold water supply section, 30... Cold water collection section, 32... Honeycomb core body, 34... Porous plate, 36... Collection body , 38... honeycomb core material, 40... fine water droplet removal section, 50... reheating coil (reheating means), 60... charging section, 62... through hole,
64... Discharge counter electrode, 66... Pointed discharge needle, 68
...Discharge electrode, 70...Blower fan (air blowing means),
90...Ozone sterilization tank (sterilization means), 93...Ozone aeration section, 94...Ozone generation section, 94'...
Ultraviolet sterilizer, 110... Irradiated object, 120...
…Luminous body.

Claims (1)

【特許請求の範囲】 1 下部又は別個に温度調整手段により温度調整
される水を収容する冷却水槽を設け、かつ、その
上部側方に空気流入口を開口すると共に、上部に
空気流出口を開口する筒状の空気清浄装置本体
と、上記空気清浄装置本体内の空気流入口と空気
流出口の中間部に配設される冷水供給部と、上記
冷水供給部の下方上流側に水平状に配設される冷
却捕集部と、上記冷水供給部の上方下流側に向つ
て順次配設される微細水滴除去部及び再熱手段と
を備え、上記空気流入口の上流側に荷電部を設け
ると共に、送風手段を介して室の吸込口に接続
し、上記空気流出口を上記室の吹出口に接続して
成り、上記冷却捕集部が、多孔板と、この多孔板
の下面に配設されるハニカムコア体とで構成され
る1組又は複数組の捕集体であり、上記荷電部
が、複数の透孔を穿設する放電対極と、上記各透
孔の中心に位置する複数の先尖状放電針を突設す
る放電極とで構成されると共に、上記冷却補集部
が、上記荷電部の放電極と反対極に通電されて成
ることを特徴とする湿式空気清浄装置。 2 温度調整手段が冷却水槽の上部又は内部に配
設される冷却コイルである特許請求の範囲第1項
記載の湿式空気清浄装置。 3 ハニカムコア体がその透孔同士が互いに偏倚
する複数の積層されたハニカムコア素材にて構成
される特許請求の範囲第1項記載の湿式空気清浄
装置。 4 下部又は別個に温度調整手段により温度調整
される水を収容する冷却水槽を設け、かつ、その
上部側方に空気流入口を開口すると共に、上部に
空気流出口を開口する筒状の空気清浄装置本体
と、上記空気清浄装置本体内の空気流入口と空気
流出口の中間部に配設される冷水供給部と、上記
冷水供給部の下方上流側に水平状に配設される冷
却捕集部と、上記冷水供給部の上方下流側に向つ
て順次配設される微細水滴除去部及び再熱手段
と、上記冷却水槽内の冷却水を殺菌処理する殺菌
手段とを備え、上記空気流入口の上流側に荷電部
を設けると共に、送風手段を介して室の吸込口に
接続し、上記空気流出口を上記室の吹出口に接続
して成り、上記冷却捕集部が、多孔板と、この多
孔板の下面に配設されるハニカムコア体とで構成
される1組又は複数組の捕集体であり、上記荷電
部が、複数の透孔を穿設する放電対極と、上記各
透孔の中心に位置する複数の先尖状放電針を突設
する放電極とで構成されると共に、上記冷却捕集
部が、上記荷電部の放電極と反対極に通電されて
成ることを特徴とする湿式空気清浄装置。 5 温度調整手段が冷却水槽の上部又は内部に配
設される冷却コイルである特許請求の範囲第4項
記載の湿式空気清浄装置。 6 ハニカムコア体がその透孔同士が互いに偏倚
する複数の積層されたハニカムコア素材にて構成
される特許請求の範囲第4項記載の湿式空気清浄
装置。 7 殺菌手段が、冷却水槽内又は冷却水槽と接続
する水槽内に配設されるオゾン曝気部と、このオ
ゾン曝気部にオゾン空気を供給するオゾン発生器
とで構成される特許請求の範囲第4項記載の湿式
空気清浄装置。 8 殺菌手段が、冷却水槽内又は冷却水槽と接続
する水槽内に配設される酸化チタン製被照射体
と、この被照射体に光を照射する発光体とで構成
されるオゾン発生器である特許請求の範囲第4項
記載の湿式空気清浄装置。 9 殺菌手段が冷却水槽内又は冷却水槽と接続す
る水槽内に配設されるオゾン曝気部と、このオゾ
ン曝気部にオゾン空気を供給するオゾン発生器
と、上記冷却水槽又は水槽内に配設されるオゾン
分解部とを備える特許請求の範囲第4項記載の湿
式空気清浄装置。 10 殺菌手段が、冷却水槽内又は冷却水槽と接
続する水槽内に配設される酸化チタン製被照射体
と、の被照射体に光を照射する発光体とで構成さ
れるオゾン発生器と、上記冷却水槽又は水槽内に
配設されるオゾン分解部とを備える特許請求の範
囲第4項記載の湿式空気清浄装置。 11 オゾン分解部が加熱コイルである特許請求
の範囲第9項又は第10項記載の湿式空気清浄装
置。 12 オゾン分解部が発光体である特許請求の範
囲第9項又は第10項記載の湿式空気清浄装置。 13 殺菌手段が、冷却水槽内又は冷却水槽と接
続する水槽内に配設される紫外線殺菌装置である
特許請求の範囲第4項記載の湿式空気清浄装置。
[Scope of Claims] 1. A cooling water tank containing water whose temperature is adjusted by a temperature adjustment means in the lower part or separately, and an air inlet is opened on the side of the upper part, and an air outlet is opened in the upper part. a cylindrical air purifier main body; a cold water supply section disposed in the middle between the air inlet and air outlet in the air purifier main body; and a cold water supply section disposed horizontally below and upstream of the cold water supply section. a cooling collection section provided therein, a fine water droplet removing section and a reheating means arranged sequentially toward the upper downstream side of the cold water supply section, and a charging section provided upstream of the air inflow port; , connected to the inlet of the chamber via an air blowing means, and connected the air outlet to the outlet of the chamber, and the cooling collection section is arranged on a perforated plate and a lower surface of the perforated plate. one or more sets of collecting bodies, each consisting of a honeycomb core body in which the charging section has a plurality of through holes, a discharge counter electrode having a plurality of through holes, and a plurality of tips located at the center of each of the through holes; 1. A wet air purifying device comprising a discharge electrode having a discharge needle projecting therefrom, and wherein the cooling collecting section is energized to a pole opposite to the discharge electrode of the charging section. 2. The wet air purifying device according to claim 1, wherein the temperature adjustment means is a cooling coil disposed above or inside the cooling water tank. 3. The wet air purifying device according to claim 1, wherein the honeycomb core body is composed of a plurality of laminated honeycomb core materials whose through holes are offset from each other. 4. A cylindrical air purifier which is provided with a cooling water tank containing water whose temperature is adjusted by a temperature adjustment means at the bottom or separately, and which has an air inlet at the side of the upper part and an air outlet at the top. A device main body, a cold water supply section disposed between an air inlet and an air outlet in the air purifying device main body, and a cooling collection disposed horizontally below and upstream of the cold water supply section. a part, a fine water droplet removing part and a reheating means which are sequentially disposed toward the upper downstream side of the cold water supply part, and a sterilizing means for sterilizing the cooling water in the cooling water tank, and the air inlet A charging section is provided on the upstream side of the chamber, and the charging section is connected to the inlet of the chamber via a blowing means, and the air outlet is connected to the outlet of the chamber, and the cooling collection section is connected to the perforated plate; A honeycomb core body disposed on the lower surface of the perforated plate is one or more sets of collectors, and the charging section is a discharge counter electrode having a plurality of through holes, and each of the through holes. and a discharge electrode protruding from a plurality of pointed discharge needles located at the center of the charging section, and the cooling collection section is energized to a pole opposite to the discharge electrode of the charging section. A wet air purification device. 5. The wet air purifying device according to claim 4, wherein the temperature adjusting means is a cooling coil disposed above or inside the cooling water tank. 6. The wet air purifying device according to claim 4, wherein the honeycomb core body is composed of a plurality of laminated honeycomb core materials whose through holes are offset from each other. 7. Claim 4, in which the sterilization means comprises an ozone aeration section disposed within the cooling water tank or a water tank connected to the cooling water tank, and an ozone generator that supplies ozone air to the ozone aeration section. Wet air purifier as described in section. 8. The sterilization means is an ozone generator consisting of a titanium oxide irradiated object disposed in a cooling water tank or a water tank connected to the cooling water tank, and a light emitter that irradiates the irradiated object with light. A wet air cleaning device according to claim 4. 9. An ozone aeration section in which the sterilization means is arranged in a cooling water tank or in a water tank connected to the cooling water tank, an ozone generator that supplies ozone air to this ozone aeration section, and an ozone generator arranged in the cooling water tank or in the water tank. The wet air cleaning device according to claim 4, comprising an ozone decomposition section. 10. An ozone generator in which the sterilization means is composed of a titanium oxide irradiated body disposed in a cooling water tank or a water tank connected to the cooling water tank, and a light emitter that irradiates the irradiated body with light; 5. The wet air purifying device according to claim 4, further comprising: the cooling water tank or an ozone decomposition unit disposed within the water tank. 11. The wet air cleaning device according to claim 9 or 10, wherein the ozone decomposition unit is a heating coil. 12. The wet air cleaning device according to claim 9 or 10, wherein the ozone decomposition part is a light emitter. 13. The wet air purifying device according to claim 4, wherein the sterilizing means is an ultraviolet sterilizer disposed in a cooling water tank or in a water tank connected to the cooling water tank.
JP62104742A 1987-04-30 1987-04-30 Wet air purifier Granted JPS63270521A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62104742A JPS63270521A (en) 1987-04-30 1987-04-30 Wet air purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62104742A JPS63270521A (en) 1987-04-30 1987-04-30 Wet air purifier

Publications (2)

Publication Number Publication Date
JPS63270521A JPS63270521A (en) 1988-11-08
JPH0518609B2 true JPH0518609B2 (en) 1993-03-12

Family

ID=14388948

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62104742A Granted JPS63270521A (en) 1987-04-30 1987-04-30 Wet air purifier

Country Status (1)

Country Link
JP (1) JPS63270521A (en)

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Publication number Priority date Publication date Assignee Title
NL1001522C2 (en) * 1995-10-30 1997-05-02 Cleyera Corp N V Device for removing dust from objects to be treated.
US7160362B2 (en) 2001-06-26 2007-01-09 Nichias Co., Ltd. Method and device for cleaning air
JP5040612B2 (en) * 2007-11-22 2012-10-03 ダイキン工業株式会社 Air purification device
JP5733337B2 (en) * 2013-06-04 2015-06-10 三菱電機株式会社 Deodorizing device
CN104338398A (en) * 2014-09-17 2015-02-11 国电新能源技术研究院 Liquid membrane dust removal system and method for achieving liquid membrane dust removal by use of liquid membrane dust removal system
CN104235866A (en) * 2014-09-17 2014-12-24 国电新能源技术研究院 Liquid film energy saving-dust removal system and method for realizing liquid film energy saving-dust removal by using system
JP6325475B2 (en) * 2015-03-18 2018-05-16 株式会社東芝 Gas recycling apparatus, additive manufacturing apparatus, and additive manufacturing method
JP7163139B2 (en) * 2018-10-31 2022-10-31 住友金属鉱山エンジニアリング株式会社 electric dust collector
CN109939826A (en) * 2019-04-26 2019-06-28 内蒙古正能化工集团有限公司 Electrical tar precipitator is used in a kind of production and processing of semi-coke
KR102506526B1 (en) * 2021-10-22 2023-03-06 주식회사 피티씨 Duct having air purifier

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JPS5256460A (en) * 1975-11-04 1977-05-09 Nippon Earo Piyuuru Kk Exhaust gas cleaner

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