JP5787136B2 - Air purification device - Google Patents

Air purification device Download PDF

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JP5787136B2
JP5787136B2 JP2011085577A JP2011085577A JP5787136B2 JP 5787136 B2 JP5787136 B2 JP 5787136B2 JP 2011085577 A JP2011085577 A JP 2011085577A JP 2011085577 A JP2011085577 A JP 2011085577A JP 5787136 B2 JP5787136 B2 JP 5787136B2
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air
purified water
filler
water
packed tower
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JP2012217581A (en
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鈴木 良延
良延 鈴木
毅 白谷
毅 白谷
正幸 小松原
正幸 小松原
弥 長谷部
弥 長谷部
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Shimizu Corp
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本発明はクリーンルームを対象としてその室内空気を浄化するための空気浄化装置に関する。   The present invention relates to an air purification device for purifying indoor air for a clean room.

この種の空気浄化装置としては、たとえば特許文献1に示されるように、多段水スプレー方式によってクリーンルーム内の有機物を除去し、清浄化した空気をクリーンルームに戻す構成のものが一般的である。   As this type of air purifying apparatus, as shown in Patent Document 1, for example, an apparatus having a configuration in which organic substances in a clean room are removed by a multistage water spray system and the cleaned air is returned to the clean room.

特許第3941029号公報Japanese Patent No. 3941029

上記従来の空気浄化装置は、
・液ガス比(処理対象空気量に対する浄化水所要量の比)がたとえば3〜4L/m3程度と大きく、しかも多量の浄化水を循環使用するためにポンプ動力に要するエネルギー使用量が大きい、
・液ガス比が大きいにも関わらず除去効率が必ずしも良くない、
・空気中の有機物を水で除去する場合、微生物の繁殖が著しくメンテナンス費用が嵩む、
・微生物対策として配管経路に水フィルタを設置したり、循環水槽に殺菌灯が必要となるなど、除去装置が複雑になりコスト高である、
といった問題がある。
The above conventional air purification device is
・ Liquid gas ratio (ratio of required amount of purified water to the amount of air to be treated) is large, for example, about 3-4L / m 3 , and energy consumption required for pump power is large for circulating a large amount of purified water.
・ Even though the liquid gas ratio is large, the removal efficiency is not always good.
・ When organic substances in the air are removed with water, the growth of microorganisms is significant and maintenance costs increase.
-As a countermeasure against microorganisms, a water filter is installed in the piping path, a germicidal lamp is required in the circulating water tank, and the removal device becomes complicated and expensive.
There is a problem.

上記事情に鑑み、本発明はイニシャルコストおよびランニングコストの軽減を図りつつ優れた浄化効果の得られる有効適切な空気浄化装置を提供することを目的とする。   In view of the above circumstances, an object of the present invention is to provide an effective and appropriate air purifying device capable of obtaining an excellent purifying effect while reducing initial cost and running cost.

請求項1記載の発明は、クリーンルームを対象としてその室内空気を浄化するための空気浄化装置であって、処理対象空気を下部から導入し上部から導出する充填塔と、前記充填塔内に充填されて処理対象空気が接触しつつ上向き流として通過可能かつ浄化水を保水可能な親水性を有する充填材と、前記充填材の上方から浄化水を噴霧して該浄化水を前記充填材に保水せしめる浄化水供給機構とを具備してなり、処理対象空気を前記充填材に接触させつつ前記充填塔内を通過させることにより、処理対象空気中の汚染物質を前記充填材が保水している浄化水に溶解せしめて処理対象空気を浄化する構成とし、前記充填材は、布材とメッシュ材とを熱融着してなる成型布と、メッシュ材を波形に成型してなるスペーサとが交互に積層されてなり、前記成型布と前記スペーサとが縦姿勢とされた状態で前記充填塔内に配置されていて、前記スペーサに形成されている波形が水平な横波とされていることを特徴とする。 The invention according to claim 1 is an air purifying apparatus for purifying indoor air for a clean room, a packed tower for introducing the air to be treated from the lower part and leading out from the upper part, and the packed tower is filled with the air. A hydrophilic filler capable of passing as an upward flow while being in contact with the air to be treated and capable of retaining purified water, and spraying purified water from above the filler to retain the purified water in the filler. Purified water comprising a purified water supply mechanism, wherein the filler retains contaminants in the treatment target air by passing the treatment target air in contact with the filler while passing through the packed tower. The filler is composed of a fabric formed by heat-sealing a cloth material and a mesh material, and a spacer formed by forming the mesh material into a corrugated shape alternately. Layered Wherein the molding fabric and the spacer is in a state of being a vertical posture is disposed in the packed tower, a waveform which is formed on the spacer is characterized in that there is a horizontal transverse waves.

請求項2記載の発明は、請求項1記載の空気浄化装置であって、前記浄化水供給機構はオゾン水を含む浄化水を供給可能に構成されていることを特徴とする。 According to a second aspect of the invention, an air purification device according to claim 1, wherein the purified water supply mechanism is characterized by being configured to be capable of supplying purified water containing ozone water.

本発明の空気浄化装置は、充填塔内に充填した充填材に浄化水を保水せしめ、その充填材に処理対象空気を接触させつつ通過させることによって、汚染物質を充填材が保水している浄化水に溶解させて除去するので、優れた浄化性能が得られることはもとより、従来一般の水スプレー方式の浄化装置に比べて構成が簡便であり、また少量の浄化水を充填材に対して単に噴霧すれば良いので浄化水の所要水量が格段に少なくて済み、そのためのポンプ動力も大幅に削減でき、したがってイニシャルコストおよびランニングコストを十分に軽減できるものである。
特に、浄化水にオゾン水を添加可能に構成することによって微生物の繁殖も有効に防止することが可能である。
The air purification apparatus of the present invention is a purification in which the filler retains the pollutant by allowing purified water to be retained in the packing material packed in the packed tower and passing the treatment target air in contact with the packing material. Since it is removed by dissolving in water, it has a simple structure compared to conventional water spray type purification devices, as well as excellent purification performance, and a small amount of purified water is simply added to the filler. Since spraying is sufficient, the amount of water required for the purified water can be remarkably reduced, and the pump power for that purpose can be greatly reduced. Therefore, the initial cost and running cost can be sufficiently reduced.
In particular, by allowing ozone water to be added to the purified water, it is possible to effectively prevent the growth of microorganisms.

本発明の実施形態である空気浄化装置およびそれを備えた空調設備全体の概要を示す図である。It is a figure which shows the outline | summary of the air purification apparatus which is embodiment of this invention, and the whole air conditioning equipment provided with the same. 同、空気浄化装置における充填材の概要を示す図である。It is a figure which shows the outline | summary of the filler in an air purifier. 同、空気浄化装置の実施例による効果を示す図である。It is a figure which shows the effect by the Example of an air purifier. 同、空気浄化装置の実施例による効果を示す図である。It is a figure which shows the effect by the Example of an air purifier.

本発明の空気浄化装置の実施形態を図1〜図4を参照して説明する。
図1は本発明の空気浄化装置10を備えた空調設備1の全体概略構成を示すものである。この空調設備1はクリーンルームを対象とするもので、図1に示すように本実施形態の空気浄化装置10の前段および後段に一次空調機2および二次空調機5を備え、処理対象空気であるクリーンルームからのリターン空気RAを一次空調機2においてHEPAフィルタ3に通して微生物粒子を除去するとともに、冷却コイル4に通して露点温度まで冷却した後、本実施形態の空気浄化装置10に導入して汚染物質を除去し、それを通過して浄化された空気を二次空調機5が備えるファン6により送風してHEPAフィルタ7に通すとともに必要に応じて加熱コイル8により所望温度に調整したうえで、給気SAとしてクリーンルームに戻るように循環させることを基本とする。
An embodiment of an air purification device of the present invention will be described with reference to FIGS.
FIG. 1 shows an overall schematic configuration of an air conditioning equipment 1 provided with an air purification device 10 of the present invention. This air-conditioning equipment 1 is intended for a clean room. As shown in FIG. 1, the air-conditioning equipment 1 includes a primary air-conditioner 2 and a secondary air-conditioner 5 at the front and rear stages of the air purification apparatus 10 according to the present embodiment, and is air to be processed. The return air RA from the clean room is passed through the HEPA filter 3 in the primary air conditioner 2 to remove microbial particles, and is cooled to the dew point temperature through the cooling coil 4 and then introduced into the air purification device 10 of the present embodiment. After removing the pollutant, the air purified by passing through it is blown by the fan 6 provided in the secondary air conditioner 5 and passed through the HEPA filter 7 and adjusted to the desired temperature by the heating coil 8 as necessary. Basically, the supply air SA is circulated back to the clean room.

上記の空調設備1に備えられている本実施形態の空気浄化装置10は、処理対象空気としてのリターン空気RAを下部から導入し上向き流として上部から導出する充填塔11と、充填塔11内に充填されて処理対象空気が接触しつつ通過可能かつ浄化水を保水可能な親水性を有する充填材12と、その充填材12の上方から浄化水を噴霧して充填材12に浄化水を保水せしめる浄化水供給機構20とを具備するものである。
なお、図示例の充填塔11内には最下部に整流板30が設置され、最上部にはエリミネータ31が設置されている。また、充填塔11の下方には充填材12から流下ないし滴下する浄化水を受けて回収するための排水槽32が設けられている。
The air purification apparatus 10 of the present embodiment provided in the air conditioning facility 1 includes a packed tower 11 that introduces return air RA as processing target air from the lower part and leads out from the upper part as an upward flow, The filler 12 having hydrophilicity that can be passed while being in contact with the air to be treated and can retain purified water, and spraying purified water from above the filler 12 to cause the filler 12 to retain purified water. And a purified water supply mechanism 20.
In the packed tower 11 shown in the figure, a rectifying plate 30 is installed at the bottom and an eliminator 31 is installed at the top. A drainage tank 32 is provided below the packed tower 11 for receiving and recovering purified water flowing down or dripping from the packing material 12.

本実施形態の空気浄化装置10において用いる充填材12としては、図2(a)に示すように、ポリエステルからなる布材13aとポリプロピレンからなるメッシュ材13bとを一体に熱融着してなる成型布13と、ポリプロピレンからなるメッシュ材を波形に成型してなるスペーサ14とが交互に積層されてなるもので、処理対象空気が十分に接触しつつかつ低圧力損失で支障なく通過可能なものである。   As the filler 12 used in the air purifying apparatus 10 of the present embodiment, as shown in FIG. 2A, a molding formed by integrally heat-bonding a cloth material 13a made of polyester and a mesh material 13b made of polypropylene. The fabric 13 and the spacers 14 formed by molding a mesh material made of polypropylene into a corrugated shape are alternately laminated, and the air to be treated can pass through without any problem with low pressure loss while being in sufficient contact. is there.

上記のポリエステルからなる布材13aとしては、糸の撚り数が大きく、布の織り方を梨地組織とし、布の仕上げ工程で溶解減量化を図り、空隙率を高くすることで親水性に優れるポリエステル布が好適に採用可能である。
なお、同様に親水性に優れる布材として木綿材を用いることも考えられるが、本実施形態で使用する充填材は親水性のみならずオゾンに対する耐久性も必要であるので、その点で木綿材は適当ではなく上記のようにポリエステル布が最適である。
As the cloth material 13a made of the above polyester, a polyester having a high hydrophilicity by increasing the number of yarn twists, making the cloth weave a satin texture, reducing the amount of dissolution in the cloth finishing process, and increasing the porosity. A cloth can be suitably employed.
Similarly, it is possible to use a cotton material as a cloth material having excellent hydrophilicity. However, the filler used in the present embodiment needs not only hydrophilic property but also durability against ozone. Is not suitable, and a polyester cloth is optimal as described above.

そして、本実施形態では、図2(a)に示すように上記の成型布13と上記のスペーサ14とをいずれも縦姿勢とし、かつスペーサ14に形成されている波形を水平な横波14aとした状態で(つまり波形を水平横方向に形成した状態で)、それらを交互に積層して(b)に示すように底部に保持メッシュ15aを有する角形筒状の収納容器15内に収納することにより、それら成型布13とスペーサ14とを多重に積層した1ユニットの充填材12を構成し、それを充填塔11内に交換可能な状態で装着するようにしている。
なお、スペーサ14に形成されている波形を鉛直な縦波として形成することでも良く、その場合は処理対象空気が縦波に沿ってそのまま上方に流れるので圧力損失の点では有利であるが、上記のように波形を横波14aとして形成した方が浄化水の保水性の点で有利であるし、また処理対象空気に対する充填材12の接触面積をより大きく確保できるので、その点で上記のように波形を横波14aとすることが好適である。
And in this embodiment, as shown to Fig.2 (a), both said shaping | molding cloth 13 and said spacer 14 are made into the vertical attitude | position, and the waveform currently formed in the spacer 14 was made into the horizontal transverse wave 14a. In a state (that is, in a state where the waveform is formed in the horizontal and horizontal directions), they are alternately stacked and stored in a rectangular cylindrical storage container 15 having a holding mesh 15a at the bottom as shown in (b). 1 unit of the packing material 12 in which the molding cloth 13 and the spacer 14 are laminated in multiple layers is configured, and the packing material 11 is mounted in a replaceable state in the packed tower 11.
The waveform formed in the spacer 14 may be formed as a vertical longitudinal wave. In this case, the air to be treated flows upward as it is along the longitudinal wave, which is advantageous in terms of pressure loss. Thus, it is advantageous to form the waveform as a transverse wave 14a in terms of water retention capacity of the purified water, and a larger contact area of the filler 12 with the air to be treated can be ensured. The waveform is preferably the transverse wave 14a.

一方、浄化水供給機構20は、熱交換器21と、給水ポンプ22と、オゾン水発生機23と、噴霧ノズル24とを具備し、熱交換器21によって処理対象空気の露点温度まで冷却された浄化水を給水ポンプ22によってオゾン発生機23に通し、オゾン水を添加した浄化水を給水管路25によって噴霧ノズル24に供給して充填材12の上方から噴霧することによって、オゾン水を含む浄化水を充填材12に保水せしめるようになっている。   On the other hand, the purified water supply mechanism 20 includes a heat exchanger 21, a water supply pump 22, an ozone water generator 23, and a spray nozzle 24, and is cooled by the heat exchanger 21 to the dew point temperature of the processing target air. Purified water containing ozone water is supplied by passing purified water through the ozone generator 23 by the feed water pump 22 and supplying the purified water to which the ozone water has been added to the spray nozzle 24 through the feed water line 25 and spraying from above the filler 12. Water is retained in the filler 12.

なお、上記のオゾン発生機23としては、浄化水を直接的に電解してオゾンを発生させる方式のものが好適に採用可能であるが、気中の酸素をオゾン化して浄化水に溶解させる方式のものも採用可能である。
また、充填塔11へ給水する浄化水中のオゾン濃度はたとえば1.5〜5ppm程度の低濃度で良く、オゾン水を浄化水に対して必ずしも常時連続的に添加することなく間欠的ないし断続的に添加することでも良いが、いずれにしてもオゾン水の添加量やその濃度を調整可能としておくことが好ましい。そのためには、図示例のようにオゾン水発生機23にバイパス管路26およびそれを開閉する電磁弁27を備えておいて、オゾン水発生機23を間欠的ないし断続的に運転して浄化水へのオゾン水の添加量やその濃度を最適に調整するように構成としておくと良い。あるいは、それに代えて、オゾン水を貯留するオゾン水槽を別途設けておいて、そこから浄化水に対してオゾン水を適宜供給することによってオゾン水の添加量や濃度を調整するようにしても良い。
In addition, as the above-described ozone generator 23, a system that generates ozone by directly electrolyzing purified water can be suitably employed, but a system that converts atmospheric oxygen into ozone and dissolves it in purified water. Can also be adopted.
Moreover, the ozone concentration in the purified water supplied to the packed tower 11 may be a low concentration of about 1.5 to 5 ppm, for example, and ozone water is not always added continuously to the purified water, but is added intermittently or intermittently. In any case, it is preferable that the amount of ozone water added and its concentration be adjustable. For this purpose, the ozone water generator 23 is provided with a bypass pipe 26 and an electromagnetic valve 27 for opening and closing the ozone water generator 23 as shown in the figure, and the ozone water generator 23 is operated intermittently or intermittently to produce purified water. It is preferable that the amount of ozone water added and the concentration thereof be adjusted optimally. Alternatively, an ozone water tank for storing ozone water may be separately provided, and the amount and concentration of ozone water may be adjusted by appropriately supplying ozone water to the purified water therefrom. .

上記構成の空気浄化装置10は、充填塔11内において処理対象空気が上向き流として充填材12を通過する際に、処理対象空気中の汚染物質が充填材12に保水されている浄化水に自ずと接触し、それにより汚染物質が浄化水に溶解して除去されることにより処理対象空気が浄化される。
すなわち、処理対象空気であるクリールームからのリターン空気RAは一次空調機2から充填塔11の下部に導入され、整流板30により整流されて均一流となって上方に向かって流れて充填材12を通過するが、その際に浄化水を保水していて濡れ面となっている充填材12の表面に接触して汚染物質(特に有機物)が浄化水に溶解し、それにより処理対象空気が浄化される。
浄化された空気はエリミネータ31により微細な水滴が除去されて充填塔11の上部から導出され、二次空調機5によりクリーンルームに循環する。
一方、充填材12に噴霧された浄化水は、充填材12に保水された状態で次第に流下ないし滴下していきつつ処理対象空気と向流接触して上記のように汚染物質を溶解し、汚染物質を溶解した浄化水は最終的には充填塔11の下部から排水槽32に回収されて適宜処理され排水される。
When the air to be treated passes through the filler 12 as an upward flow in the packed tower 11, the air purification apparatus 10 having the above configuration naturally has the contaminants in the air to be treated held in the purified water retained in the filler 12. By contacting, the pollutant is dissolved and removed in the purified water, so that the air to be treated is purified.
That is, the return air RA from the clean room, which is the air to be treated, is introduced from the primary air conditioner 2 to the lower portion of the packed tower 11, rectified by the rectifying plate 30 and flows upward as a uniform flow, and flows upward. At that time, the purified water is retained and in contact with the surface of the filler 12 which is a wet surface, pollutants (especially organic substances) dissolve in the purified water, thereby purifying the air to be treated. Is done.
Fine air droplets are removed from the purified air by the eliminator 31, and the purified air is led out from the upper part of the packed tower 11, and circulates to the clean room by the secondary air conditioner 5.
On the other hand, the purified water sprayed on the filler 12 gradually flows down or drops while being retained in the filler 12, and countercurrently contacts with the air to be treated to dissolve the contaminants as described above. The purified water in which the substance is dissolved is finally collected from the lower part of the packed tower 11 into the drainage tank 32, appropriately treated and drained.

本実施形態の空気浄化装置10によれば、処理対象空気を充填材12に保水せしめた浄化水に接触させてその浄化水に汚染物質を溶解させて除去するので、充填材12に対して少量の浄化水を噴霧して保水させることのみで、以下に示す実施例で実証されるように優れた浄化効果が得られるものである。   According to the air purification device 10 of the present embodiment, the processing target air is brought into contact with the purified water retained in the filler 12 and the contaminants are dissolved and removed in the purified water. Only by spraying the purified water to retain the water, an excellent purification effect can be obtained as demonstrated in the following examples.

(実施例1)
梨地組織のポリエステルからなる布材13aと20メッシュのポリプロピレンからなるメッシュ材13bとを熱融着させた成型布13と、10メッシュのポリプロピレンからなるメッシュ材に横波14aを形成したスペーサ14とを積層した充填材12を用いる。充填材12の断面サイズは294mm×294mmとし、その長さ(高さ)を300mm、600mm、900mm、1200mmの4種とした。
処理対象空気量を7.9m3/min、浄化水の噴霧量を0.62L/min(液ガス比は約0.08L/m3)、充填塔11内の通過風速を1.5m/sとした。
Example 1
Laminated fabric 13a made of polyester having a satin texture and mesh material 13b made of 20 mesh polypropylene are heat-sealed, and spacer 14 having a transverse wave 14a formed on a mesh material made of 10 mesh polypropylene. The filler 12 made is used. The cross-sectional size of the filler 12 was 294 mm × 294 mm, and its length (height) was four types of 300 mm, 600 mm, 900 mm, and 1200 mm.
The amount of air to be treated was 7.9 m 3 / min, the amount of purified water sprayed was 0.62 L / min (liquid / gas ratio was about 0.08 L / m 3 ), and the passing air speed in the packed tower 11 was 1.5 m / s.

浄化対象の汚染物質を空気中の有機溶剤PGMEA(プロピレングリコールモノメチルエーテルアセテート)成分とした場合における除去性能とドレン温度との関係を図3に示す。図中の直線は充填材12の長さが300mm、900mm、1200mmの場合における回帰直線である。
本実施例では、ドレン温度が13.5℃の場合において、充填材長さ900mmで除去率80%、充填材長さ1200mmで除去率85%が得られた。また、充填材長さ600mmでは70%程度、300mmでも60%程度の除去率が得られた。
有機溶剤の気液平衡におけるヘンリー定数は吸収液体温度が低いほど小さくなることが知られているので、本実施例による測定結果の除去率はドレン温度に依存しており、吸収理論に整合していることが確認された。
FIG. 3 shows the relationship between the removal performance and the drain temperature when the pollutant to be purified is an organic solvent PGMEA (propylene glycol monomethyl ether acetate) component in the air. The straight lines in the figure are regression lines when the length of the filler 12 is 300 mm, 900 mm, and 1200 mm.
In this example, when the drain temperature was 13.5 ° C., a removal rate of 80% was obtained at a filler length of 900 mm, and a removal rate of 85% was obtained at a filler length of 1200 mm. In addition, a removal rate of about 70% was obtained when the filler length was 600 mm, and about 60% even when the length was 300 mm.
Since it is known that the Henry's constant in the vapor-liquid equilibrium of the organic solvent becomes smaller as the absorbing liquid temperature is lower, the removal rate of the measurement result according to this example depends on the drain temperature and is consistent with the absorption theory. It was confirmed that

なお、上記実施例1に対する比較例として、充填材サイズが同じく294mm×294mm、長さ900mmのユニットに一般の充填塔で使用される汎用のボール状充填材(φ27mm)を充填して同一条件で処理した場合、除去率は35%程度に過ぎず、本発明の空気除去装置の除去性能は格段に優れていることが確認された。   As a comparative example with respect to Example 1 above, a unit of the same size of 294 mm × 294 mm and a length of 900 mm is filled with a general-purpose ball-shaped filler (φ27 mm) used in a general packed tower, under the same conditions. When treated, the removal rate was only about 35%, and it was confirmed that the removal performance of the air removal device of the present invention was remarkably excellent.

(実施例2)
図1に示した空気浄化装置10において充填材12は上記実施例1と同様のものとし、充填材12の断面サイズを300mm×300mm、長さ900mmとしたユニットを8本設置し、処理空気量65.9m3/min、浄化水の噴霧量6.2L/min(液ガス比は約0.09L/m3)、塔内風速を1.5m/sとした場合、ドレン温度10℃においてPGMEA成分の除去率は90%であり、実施例1と同様に従来の充填材による場合に比べて格段に優れた除去率が得られた。
(Example 2)
In the air purifying apparatus 10 shown in FIG. 1, the filler 12 is the same as that of the first embodiment, and eight units each having a cross-sectional size of 300 mm × 300 mm and a length of 900 mm are installed. The removal rate of PGMEA components at a drain temperature of 10 ° C with 65.9m 3 / min, purified water spray rate of 6.2L / min (liquid / gas ratio is about 0.09L / m 3 ), and the tower wind speed is 1.5m / s The removal rate was 90%, and a remarkably superior removal rate was obtained as compared with the case of the conventional filler as in Example 1.

(実施例3)
図1に示した空気浄化装置10において充填材12は実施例2と同様のものとし、PGMEAを含む空気処理量57.3m3/min、浄化水の噴霧量8L/min(液ガス比は約0.14L/m3)、塔内風速1.3m/sとし、オゾン水発生機23を使用してオゾン水を間欠的に噴霧した場合(濃度1.5ppmのオゾン水を含む浄化水と、オゾン水を含まない浄化水とを12時間ごとに交互に噴霧した場合)、ドレン中の微生物濃度を継続的に測定した。
その結果、図4に示すように400日間にわたって細菌濃度、真菌濃度のいずれも100cfu/mL以下であった。400日後に充填材を観察したところ、充填材は清浄で微生物の付着は全く見られなかった。このことから、濃度1.5ppmのオゾン水を間欠噴霧することで微生物繁殖を防止できることが確認できた。
(Example 3)
In the air purifying apparatus 10 shown in FIG. 1, the filler 12 is the same as that of the second embodiment, the air treatment amount containing PGMEA is 57.3 m 3 / min, the amount of purified water sprayed is 8 L / min (the liquid gas ratio is about 0.14). L / m 3 ), when the wind speed in the tower is 1.3 m / s, and ozone water is intermittently sprayed using the ozone water generator 23 (including purified water containing 1.5 ppm of ozone water and ozone water) No clarified water was sprayed every 12 hours alternately), and the microbial concentration in the drain was continuously measured.
As a result, as shown in FIG. 4, both the bacterial concentration and the fungal concentration were 100 cfu / mL or less over 400 days. When the filler was observed after 400 days, the filler was clean and did not show any microbial adhesion. From this, it was confirmed that microbial growth could be prevented by intermittently spraying ozone water with a concentration of 1.5 ppm.

以上のように、本発明の空気浄化装置は従来一般の浄化装置に比較して格段に優れた浄化性能が得られることはもとより、処理対象空気を単に充填塔11内を上向き流として通過させ、かつ充填塔11内の充填材12に対して少量の浄化水を噴霧して保水せしめるだけの簡便な構成であるので、従来一般の水スプレー方式の浄化装置に比べて構成が遙かに簡便であってイニシャルコストを軽減できるものである。   As described above, the air purification apparatus of the present invention allows the air to be treated to simply pass through the packed tower 11 as an upward flow, as well as obtaining a purification performance that is significantly superior to conventional purification apparatuses. In addition, since it has a simple configuration in which a small amount of purified water is sprayed onto the packing material 12 in the packed tower 11 to retain the water, the configuration is much simpler than a conventional water spray type purification device. Therefore, the initial cost can be reduced.

特に本発明の空気浄化装置は、従来の多段水スプレー方式の浄化装置に比べて浄化水の所要水量を大きく削減し得て効率的な運転が可能であり、したがってランニングコストを十分に軽減し得るものである。
すなわち、従来の多段水スプレー方式の浄化装置では多量の浄化水を処理対象空気に対して直接的に噴霧することで浄化効果を得るものであるから、多量の浄化水を必要とするばかりでなく多量の浄化水を循環使用するために多大なポンプ動力を必要とするのに対し、本発明の空気浄化装置は浄化水を保水せしめた充填材12に処理対象空気を接触させつつ通過させるものであり、したがって多量の浄化水を循環使用することなく少量の浄化水をワンパス方式で単に充填材12に対して補給水として噴霧するだけで十分である。
それ故に、本発明によれば浄化水の所要量を大幅に削減し得て、液ガス比を従来の3〜4L/m3程度から上記実施例のように0.08L/m3程度と従来の1/30程度にまで大幅に削減できるし、そのためのポンプ動力もわずかで済み、したがってランニングコストを十分に軽減可能である。
In particular, the air purification device of the present invention can greatly reduce the amount of water required for purified water compared to conventional multi-stage water spray type purification devices, and thus can efficiently operate, and thus can sufficiently reduce running costs. Is.
That is, the conventional multistage water spray type purification device obtains a purification effect by directly spraying a large amount of purified water onto the air to be treated, so that not only a large amount of purified water is required. While a large amount of pump power is required to circulate and use a large amount of purified water, the air purification device of the present invention allows the air to be treated to pass through the filler 12 in which the purified water is retained. Therefore, it is sufficient to spray a small amount of purified water as makeup water on the filler 12 by a one-pass method without circulating and using a large amount of purified water.
Therefore, the obtained significantly reduces the required amount of purified water according to the present invention, the liquid-to-gas ratio from a conventional 3~4L / m 3 approximately 0.08L / m 3 degree and conventional, as described above in Example It can be greatly reduced to about 1/30, and the pump power for that is also little, so the running cost can be reduced sufficiently.

しかも、上記実施形態のように浄化水供給機構20にオゾン水発生機23を備えて浄化水にオゾン水を添加可能に構成することによって、微生物の繁殖を有効に防止でき、それにより空気浄化装置10を長期にわたって連続運転することも可能であるから、この点においても保守費を軽減することができ、高度の清浄度が要求されるクリーンルームに適用する空気浄化装置として極めて有効なものである。   In addition, as in the above embodiment, the purified water supply mechanism 20 includes the ozone water generator 23 so that ozone water can be added to the purified water, thereby effectively preventing the growth of microorganisms. 10 can be continuously operated over a long period of time, so that the maintenance cost can be reduced in this respect as well, and it is extremely effective as an air purifying apparatus applied to a clean room requiring a high degree of cleanliness.

以上で本発明の実施形態について説明したが、上記実施形態はあくまで好適な一例であって本発明は上記実施形態に限定されるものでは勿論なく、本発明の要旨を逸脱しない範囲内で適宜の設計的変更や応用が可能である。   Although the embodiment of the present invention has been described above, the above embodiment is merely a preferred example, and the present invention is not limited to the above embodiment, and may be appropriately selected within the scope of the present invention. Design changes and applications are possible.

たとえば、空気浄化装置10の構成要素である充填塔11の形態や大きさ、その内部に充填する充填材12の具体的な仕様、浄化水供給機構20の構成等、各部の具体的な構成は、除去すべき汚染物質の種類や汚染程度、要求される清浄度、処理風量その他の諸条件を考慮して最適な処理を行い得るように最適設計すれば良い。   For example, the specific configuration of each part, such as the configuration and size of the packed tower 11 that is a component of the air purification device 10, the specific specifications of the packing material 12 filled therein, the configuration of the purified water supply mechanism 20, etc. The optimum design may be performed so that the optimum treatment can be performed in consideration of the types of contaminants to be removed, the degree of contamination, the required cleanliness, the amount of treatment air flow, and other conditions.

特に、浄化水供給機構20は充填材12に対して必要最小限の浄化水を噴霧してそれに保水させることが可能なものであれば良いから、その限りにおいて浄化水供給機構20の構成は任意に設計可能である。
なお、浄化水供給機構20には上記実施形態のようにオゾン水発生機23を備えることが好ましく、それにより微生物の繁殖を有効に防止できるのでそのように構成することが最適ではあるが、微生物の繁殖が想定されないような場合等においてオゾン水発生機23が不要であれば省略しても差し支えない。
In particular, the purified water supply mechanism 20 only needs to be capable of spraying the minimum amount of purified water onto the filler 12 and retaining the purified water. Can be designed.
The purified water supply mechanism 20 is preferably provided with an ozone water generator 23 as in the above embodiment, so that it is possible to effectively prevent the growth of microorganisms. If the ozone water generator 23 is not necessary, for example, in the case where the breeding of the water is not expected, it may be omitted.

また、本発明の空気浄化装置は上記実施形態のようにクリーンルームを対象とする空調設備1に組み込んで使用することが現実的であるが、必ずしもそうすることはなく、処理対象空気の循環手段を別途用意すれば本発明の空気浄化装置を単独で使用することも可能である。
勿論、本発明の空気浄化装置を上記のように空調設備に組み込む場合においても、その空調設備全体の構成は、処理対象空気を本発明の空気浄化装置に通しつつ循環させる構成とする限りにおいて任意である。
Moreover, although it is realistic to incorporate and use the air purification apparatus of this invention in the air-conditioning equipment 1 which makes a clean room the object like the said embodiment, it does not necessarily do so and the circulation means of the process target air is used. If prepared separately, the air purifier of the present invention can be used alone.
Of course, even when the air purification apparatus of the present invention is incorporated in the air conditioning equipment as described above, the configuration of the entire air conditioning equipment is arbitrary as long as the air to be treated is circulated through the air purification apparatus of the present invention. It is.

1 空調設備
2 一次空調機
3 HEPAフィルタ
4 冷却コイル
5 二次空調機
6 ファン
7 HEPAフィルタ
8 加熱コイル
10 空気浄化装置
11 充填塔
12 充填材
13 成型布
13a 布材(ポリエステル)
13b メッシュ材(ポリプロピレン)
14 スペーサ(ポリプロピレン)
14a 横波
15 収納容器
15a 保持メッシュ
20 浄化水供給機構
21 熱交換器
22 給水ポンプ
23 オゾン水発生機
24 噴霧ノズル
25 給水管路
26 バイパス管路
27 電磁弁
30 整流板
31 エリミネータ
32 排水槽
DESCRIPTION OF SYMBOLS 1 Air conditioning equipment 2 Primary air conditioner 3 HEPA filter 4 Cooling coil 5 Secondary air conditioner 6 Fan 7 HEPA filter 8 Heating coil 10 Air purifier 11 Packing tower 12 Filling material 13 Molding cloth 13a Cloth material (polyester)
13b Mesh material (polypropylene)
14 Spacer (Polypropylene)
14a Shear wave 15 Storage container 15a Holding mesh 20 Purified water supply mechanism 21 Heat exchanger 22 Water supply pump 23 Ozone water generator 24 Spray nozzle 25 Water supply line 26 Bypass line 27 Solenoid valve 30 Current plate 31 Eliminator 32 Drainage tank

Claims (2)

クリーンルームを対象としてその室内空気を浄化するための空気浄化装置であって、
処理対象空気を下部から導入し上部から導出する充填塔と、
前記充填塔内に充填されて処理対象空気が接触しつつ上向き流として通過可能かつ浄化水を保水可能な親水性を有する充填材と、
前記充填材の上方から浄化水を噴霧して該浄化水を前記充填材に保水せしめる浄化水供給機構とを具備してなり、
処理対象空気を前記充填材に接触させつつ前記充填塔内を通過させることにより、処理対象空気中の汚染物質を前記充填材が保水している浄化水に溶解せしめて処理対象空気を浄化する構成とし、
前記充填材は、布材とメッシュ材とを熱融着してなる成型布と、メッシュ材を波形に成型してなるスペーサとが交互に積層されてなり、前記成型布と前記スペーサとが縦姿勢とされた状態で前記充填塔内に配置されていて、
前記スペーサに形成されている波形が水平な横波とされていることを特徴とする空気浄化装置。
An air purification device for purifying indoor air for a clean room,
A packed tower for introducing the air to be treated from the bottom and leading from the top;
A filler having a hydrophilic property that is packed in the packed tower and can be passed as an upward flow while being in contact with the air to be treated and that can retain purified water; and
Comprising a purified water supply mechanism for spraying purified water from above the filler to retain the purified water in the filler;
A configuration for purifying the processing target air by allowing the processing target air to pass through the packed tower while being in contact with the packing material, thereby dissolving the pollutants in the processing target air in the purified water retained by the packing material. and,
The filler is formed by alternately stacking a molded cloth formed by heat-sealing a cloth material and a mesh material and a spacer formed by forming a mesh material into a corrugated shape, and the molded cloth and the spacer are vertically arranged. Arranged in the packed tower in a state of being in a posture,
An air purifier characterized in that a waveform formed on the spacer is a horizontal transverse wave .
請求項1記載の空気浄化装置であって、
前記浄化水供給機構はオゾン水を含む浄化水を供給可能に構成されていることを特徴とする空気浄化装置。
The air purification device according to claim 1 ,
The purified water supply mechanism is configured to be able to supply purified water including ozone water.
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JPH11300140A (en) * 1998-04-23 1999-11-02 Shinko Pantec Co Ltd Method of purifying air in clean room and device therefor
JP2002079037A (en) * 2000-09-08 2002-03-19 Kurita Water Ind Ltd Method for cleaning gas-liquid contact tower
JP2007252702A (en) * 2006-03-24 2007-10-04 Sanyo Electric Co Ltd Air disinfecting apparatus
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