JPH03284319A - Air treating element and water screen-type air treating device having the same - Google Patents

Air treating element and water screen-type air treating device having the same

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Publication number
JPH03284319A
JPH03284319A JP2081191A JP8119190A JPH03284319A JP H03284319 A JPH03284319 A JP H03284319A JP 2081191 A JP2081191 A JP 2081191A JP 8119190 A JP8119190 A JP 8119190A JP H03284319 A JPH03284319 A JP H03284319A
Authority
JP
Japan
Prior art keywords
water
plate
valleys
air
longitudinal grooves
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2081191A
Other languages
Japanese (ja)
Inventor
Wataru Inoue
渉 井上
Setsu Takeshita
竹下 節
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.)
BAANAA INTERNATL KK
Original Assignee
BAANAA INTERNATL KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BAANAA INTERNATL KK filed Critical BAANAA INTERNATL KK
Priority to JP2081191A priority Critical patent/JPH03284319A/en
Publication of JPH03284319A publication Critical patent/JPH03284319A/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)
  • Separation Of Particles Using Liquids (AREA)

Abstract

PURPOSE:To collect dust and to make malodorous gases absorb by laminating plates having a longitudinal recessed groove on its front and rear in the thickness direction to obtain an air treating element, erecting the recessed groove and arranging a water sprinkler above the upper surface. CONSTITUTION:The plates 12 have a cross section on which continuous mountains and valleys are alternately arranged, and a longitudinal recessed groove 12c is formed on the front and rear. Many plates 12 are laminated in the thickness direction, the grooves of the adjacent plates 12 are crossed with one another at a certain angle, and the bottom of the valley of the groove of one plate is brought into point-contact with the peak of the mountain of the groove of the adjacent plate. The air treating element thus constituted is erected so that the groove is vertically directed, and a cross section having alternate continuous mountains and valleys is formed on the upper surface. A water sprinkler 13 is arranged above the upper surface and a water receiver 14 below the lower surface. Consequently, dust and microbes are collected and malodorous gases are absorbed by the formed water screen.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、空気浄化等の空気処理に使用される空気処理
エレメント及びこのエレメントを有する水膜型空気処理
装置に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to an air treatment element used for air treatment such as air purification, and a water film type air treatment device having this element.

〈従来の技術とその課題〉 空気処理、例えば集塵浄化処理、ガスや臭気の浄化処理
、浮遊微生物の除去処理、加湿もしくは除湿処理等は、
産業上又は環境浄化のために多種多様に行なわれている
<Conventional technology and its problems> Air treatment, such as dust collection and purification treatment, gas and odor purification treatment, floating microorganism removal treatment, humidification or dehumidification treatment, etc.
A wide variety of methods are used for industrial or environmental purification purposes.

このうち、最も一般的なフィルターは集塵浄化処理を主
に行なうものであり、ダストの蓄積により清掃して再使
用をする方式が採られている。しかし、この方式は清掃
の手数がかかる外、ダストの種類によっては使用できな
い等、使用範囲が極めて限られている。
Among these, the most common type of filter is one that mainly performs dust collection and purification processing, and a method is adopted in which the dust is accumulated and then cleaned and reused. However, this method requires a lot of cleaning work and cannot be used depending on the type of dust, so its range of use is extremely limited.

別の方式として、いわゆるエアワッシャ方式がある。こ
の方式は、水滴中に空気を通すもので、ダストを水の吸
着により捕集したり、浮遊バクテリア等の微生物の捕集
や水と親和性のあるガスや臭気の捕集を行なうのである
が、水滴の大きさもまちまちでダストやバクテリアの捕
集には水滴の大きさの点から限界があり、細かな水滴の
飛散によってその水滴の気化した後は再度空気中のダス
トが生じ集塵効果がみかけ上低下する。
Another method is the so-called air washer method. This method allows air to pass through water droplets, and is used to collect dust by adsorbing water, as well as microorganisms such as floating bacteria, and gases and odors that have an affinity for water. The size of water droplets also varies, and there is a limit to the collection of dust and bacteria due to the size of the water droplets.After the water droplets are vaporized by the scattering of small water droplets, dust is generated in the air again and the dust collection effect is reduced. Appearance decreases.

また、ウォーターカーテン方式である水膜に空気を衝突
させてダストを捕集する場合には、構造上繰返して何回
も衝突させるということが困難であり、したがってエア
ワッシャ方式のような水滴の発生はないとしても捕集効
率はさほど高くならない。
In addition, when collecting dust by colliding air with a water film, which is the water curtain method, it is difficult to repeatedly collide the water film many times due to the structure, so water droplets are generated as in the air washer method. Even if there is no such thing, the collection efficiency will not be very high.

ガス・臭気の浄化に当っては、例えば活性炭に空気を触
れることにより効果的に捕集することができるが、しか
し活性炭の寿命は極めて短いという欠点がある。
In purifying gases and odors, for example, air can be effectively collected by exposing activated carbon to air, but activated carbon has the disadvantage that its lifespan is extremely short.

また、従来の加湿器に着目した場合、超音波式や水噴霧
式の如く水滴により加湿が行なわれるが、水分中のダス
トやカルシウム分も同時に空中飛散しいわゆる白粉現象
が生じてスケールの成長が生ずる。更には、水滴からガ
スに変るに必要な距離である加湿吸収距離を必要としス
ペースを要する。
In addition, when looking at conventional humidifiers, humidification is performed using water droplets such as ultrasonic type or water spray type, but dust and calcium in the moisture are also scattered in the air, causing the so-called white powder phenomenon and causing scale growth. arise. Furthermore, it requires a humidification absorption distance, which is the distance required for water droplets to change into gas, and requires space.

更に、従来クーリングタワー充填材として使用されるも
のを加湿器として使用する場合、水膜と水滴との混合型
であるが、やはり白粉の発生やバクテリア等のエアゾル
が生成する。
Furthermore, when a humidifier that is conventionally used as a cooling tower filler is used as a humidifier, although it is a mixture of water film and water droplets, white powder and aerosols such as bacteria are generated.

有効径8m未満の積層ハニカム素子を加湿器等として使
用する場合、物質移動を行なう(気化を行なう)面積は
太き(て好都合であるが、ハニカム内に浄化と加湿のた
め水膜を作ろうとするとハニカム構造上水のブリッジが
生じ易く、またハニカムフルート内の空気流にて水のブ
リッジが破れるとき水滴が飛散する。しかも、フルート
内部にてダストが粘着したり給水中の無機質分の濃度が
気化にて濃縮スラリー化する。すなわち、空気の貫流静
圧損失が上昇し寿命が短くなる。
When using a laminated honeycomb element with an effective diameter of less than 8 m as a humidifier, etc., the area for mass transfer (vaporization) is large (which is convenient), but it is difficult to create a water film within the honeycomb for purification and humidification. As a result, water bridges are likely to occur due to the honeycomb structure, and when the water bridges are broken by the air flow inside the honeycomb flutes, water droplets are scattered.Furthermore, dust may stick inside the flutes and the concentration of inorganic substances in the water supply may be reduced. It becomes a concentrated slurry through vaporization.In other words, the through-flow static pressure loss of air increases and the service life is shortened.

また、多孔質で細孔を有する膜を浸透し水分が気化する
タイプのものは、水滴の飛散は起らず都合が良いけれど
も、細孔の詰りによる効率の低下は避けられない。
In addition, a type in which water permeates through a porous membrane with pores and evaporates is advantageous because water droplets do not scatter, but a decrease in efficiency due to clogging of the pores is unavoidable.

金属又は合成樹脂の繊維によるマトリックスを使用した
加湿器にあっては、安価であるが、内部で水膜の破裂に
よる水滴が生じ、マトリックス内部で捕捉されたダスト
や微生物の除去は困難であり、詰まり白粉の生成が生ず
る。このため、静圧損失の上昇と加湿効率°の低下によ
り寿命が短い。
Humidifiers that use a matrix made of metal or synthetic resin fibers are inexpensive, but water droplets are generated due to the rupture of the water film inside the humidifier, making it difficult to remove dust and microorganisms trapped inside the matrix. Clogging results in the formation of white powder. As a result, the service life is short due to an increase in static pressure loss and a decrease in humidification efficiency.

本発明は、前述した各種の空気処理装置の問題を除去し
、洗浄が不要、水滴の発生除去、多数段の装置の設置、
短寿命、等の従来の集塵、脱ガス、脱臭、加湿、冷却で
の欠点を除去した空気処理エレメントとこのエレメント
を有する水膜型空気処理装置の提供を目的とする。
The present invention eliminates the problems of the various air treatment devices described above, eliminates the need for cleaning, eliminates water droplets, and allows installation of multiple stages of devices.
The object of the present invention is to provide an air treatment element that eliminates drawbacks such as short life in conventional dust collection, degassing, deodorization, humidification, and cooling, and a water film type air treatment device having this element.

く課題を解決するための手段〉 上述の目的を達成する本発明は、 (1)山谷が交互に連続する断面を有しかつこの山谷に
よって表側及び裏側より長手凹溝が形成される板状体を
、多数枚その厚さ方向に積層すると共に隣接する上記板
状体の上記長手凹溝をある角度有して交互に積層し、相
互に隣接する一方の板状体の上記長手凹溝を形成する谷
の底部と他方の板状体の上記長手凹溝を形成する山の頂
部とを点接触させた空気処理エレメントを特徴とし、 (2)表裏に長手凹溝を形成する板状体を厚さ方向に積
層して構成される空気処理エレメントを上記長手凹溝が
上下に立つように上面に山谷が交互に連続する断面を臨
ませ、この上面上方に散水装置を配置すると共に下面下
方に水受けである水槽を配置した水腹型空気処理装置を
特徴とする。
Means for Solving the Problems> The present invention achieves the above-mentioned objects by: (1) A plate-like body having a cross section in which peaks and valleys are continuous alternately, and in which longitudinal grooves are formed from the front side and the back side by the peaks and valleys. are laminated in the thickness direction, and the longitudinal grooves of the adjacent plate-shaped bodies are alternately stacked at a certain angle to form the longitudinal grooves of one of the mutually adjacent plate-shaped bodies. (2) The plate-like body forming the longitudinal grooves on the front and back sides has a thickness of The air treatment element, which is constructed by stacking the air treatment elements in the horizontal direction, is arranged so that the longitudinal grooves stand up and down, so that the upper surface faces a cross section with alternating peaks and valleys. It is characterized by a water belly type air treatment device with a water tank as a receiver.

〈作   用〉 積層した板状体の山谷が交互に連続する上面側から散水
することにより、長手凹溝内を点接触部分からまんべん
なく水膜が拡がり、長手凹溝の表裏両面全体を水膜を形
成しつつ水が流れ、他方処理空気は、隣接する長手凹溝
の壁に次々に衝突しながら長手凹溝の山谷を越えてわた
ることにより、集塵、脱ガス、脱臭、加湿、冷却が行な
われる。なお、この場合、水膜の表面張力により空気流
による水滴の飛散は生じない。
<Operation> By sprinkling water from the upper surface side where the peaks and troughs of the laminated plate-like bodies are continuous alternately, a water film spreads evenly within the longitudinal groove from the point contact area, and the water film covers the entire front and back surfaces of the longitudinal groove. Water flows while forming, while the treated air collides with the walls of adjacent longitudinal grooves one after another and crosses over the peaks and valleys of the longitudinal grooves, thereby collecting dust, degassing, deodorizing, humidifying, and cooling. It will be done. Note that in this case, water droplets are not scattered by the air flow due to the surface tension of the water film.

く実 施 例〉 ここで、図を参照して本発明の詳細な説明する。第1図
は空気処理装置11の全体を示すもので、山谷が交互に
連続する断面例えば波形断面を有する多数枚の板状体1
2が層状に重ね合わせられており、この板状体12の上
面上方には放出口より供給する放出管13が配置されて
おり、板状体12の波形表面に沿って流下する水を散水
する。
Embodiments Here, the present invention will be described in detail with reference to the drawings. FIG. 1 shows the entire air treatment device 11, which includes a large number of plate-like bodies 1 each having a cross section with alternating peaks and valleys, for example, a wave-shaped cross section.
2 are stacked on top of each other in a layered manner, and a discharge pipe 13 is arranged above the upper surface of this plate-like body 12 to supply water from a discharge port, and sprinkles water flowing down along the corrugated surface of the plate-like body 12. .

また、板状体12の下面下方には、水を受ける水槽14
が備えられている。この水槽14には空気処理装置11
に新鮮水を供給するための供給管15がバルブ16を介
して連通されていると共に、前述した放出管13の基端
部側が水槽14内の水に挿入される状態で固定されてい
る。また、放出管13の途中には、水槽14内の水を放
出管13の末端側へと圧送してこれを板状体12に供給
するためのポンプ17が介装されている。
Further, below the lower surface of the plate-like body 12, a water tank 14 for receiving water is provided.
is provided. This water tank 14 has an air treatment device 11.
A supply pipe 15 for supplying fresh water to the water tank 15 is connected to the water tank 15 via a valve 16, and the base end side of the discharge pipe 13 is inserted and fixed into water in the water tank 14. Further, a pump 17 is interposed in the middle of the discharge pipe 13 for pumping the water in the water tank 14 to the distal end side of the discharge pipe 13 and supplying it to the plate-shaped body 12.

したがって、供給管15より水槽14内に供給された水
は、ポンプ17の作動と共に放出管13内を流れ、板状
体12の上面上方に位置する放出管13の放出口より放
出され、板状体12の表面に沿って水膜を形成しながら
流下する。この際、図示しないダスト等より導かれた空
気18が、板状体12の隙間より流れ込み前述した水膜
の表面に衝突しながら通過することになる。
Therefore, the water supplied from the supply pipe 15 into the water tank 14 flows through the discharge pipe 13 with the operation of the pump 17, and is discharged from the discharge port of the discharge pipe 13 located above the upper surface of the plate-shaped body 12. The water flows down while forming a water film along the surface of the body 12. At this time, air 18 guided by dust or the like (not shown) flows through the gap between the plate-like bodies 12 and passes through while colliding with the surface of the water film described above.

板状体12の下流端まで達した水は、そのまま水槽14
内に流下し、供給管15より供給された新鮮水と混じり
再び放出管13へと導びかれ循環する。
The water that has reached the downstream end of the plate-shaped body 12 is directly transferred to the water tank 14.
The water flows down into the water, mixes with fresh water supplied from the supply pipe 15, and is led back to the discharge pipe 13 for circulation.

この場合、板状体12の表面に沿って流下する水は、空
気の衝突により、ダスト、ガス、臭気、微生物等を吸着
、吸収することにより汚染される。このため、ポンプ1
7の下流側の放出管13に水の一部を外部へ排出するた
めの排出管19が連通され、排出管19の途中に排出水
量の調節のためのバルブ20が介装されている。排出水
量の調節は、汚染水のダスト、ガス、臭気、微生物等の
汚染濃度にてらし、目的に応じて調節することになる。
In this case, the water flowing down along the surface of the plate-shaped body 12 is contaminated by adsorbing and absorbing dust, gas, odor, microorganisms, etc. due to air collision. For this reason, pump 1
A discharge pipe 19 for discharging part of the water to the outside is connected to the discharge pipe 13 on the downstream side of the discharge pipe 7, and a valve 20 for adjusting the amount of discharged water is interposed in the middle of the discharge pipe 19. The amount of discharged water is adjusted depending on the purpose, depending on the concentration of dust, gas, odor, microorganisms, etc. in the contaminated water.

もっとも、バイオテクノロジー、危険物扱い、放射能に
係る用途にあっては、性質上水を循環する方式でなく新
鮮水を放出管13より出すだけの方式も考えられる。
However, for applications related to biotechnology, handling of hazardous materials, and radioactivity, it is conceivable to consider a method in which fresh water is simply discharged from the discharge pipe 13 instead of a method in which water is circulated due to its nature.

また、バルブ20は排水バルブであるが、水槽14のオ
ーバフローバルブをこのバルブ20の代りに取付けても
よい。
Furthermore, although the valve 20 is a drain valve, an overflow valve for the water tank 14 may be installed in place of this valve 20.

さて、この第1図に示す空気処理装置11にあってその
エレメントを第2図以下に示す。
Now, the elements of the air treatment apparatus 11 shown in FIG. 1 are shown in FIGS. 2 and below.

第2図はエレメントの一部を切取った構造を示し、多数
枚の板状体12がその厚さ方向に積層されている。この
場合、隣接する板状体12a、12bどおしは、山谷が
交互に連続する断面(本実施例では波形断面)を有する
長手凹溝(フルート)の長手方向がある角度、例えば3
0°とか45″をなして交差するように積層される。こ
の状態は、例えば第3図に示すように板状体12aと板
状体12bとを互いに斜め方向に長手凹溝12cが位置
するように重ね合わせ、第4図に示す状態に構成するも
のである。
FIG. 2 shows a partially cut-out structure of the element, in which a large number of plate-like bodies 12 are stacked in the thickness direction. In this case, the adjacent plate-like bodies 12a and 12b are arranged at a certain angle in the longitudinal direction of a flute having a cross section in which peaks and troughs continue alternately (in this embodiment, a wavy cross section).
They are stacked so as to intersect with each other at an angle of 0° or 45''. In this state, for example, as shown in FIG. They are superimposed as shown in FIG. 4 to form the structure shown in FIG.

実線を山の頂部、破線を谷の底部とした第5図の如く、
右下りの表側板状体12aに対して左下りの裏側板状体
12bが、黒点の箇所で点接触することになる。
As shown in Figure 5, where the solid line is the top of the mountain and the broken line is the bottom of the valley,
The back side plate-like body 12b, which is downward to the left, makes point contact with the front plate-like body 12a, which is downward to the right, at the black dots.

この結果、波形断面側から水を散水すると板状体12の
表裏を伝って水が流下する際、点接触部分で水が枝分か
れして分流し、板状体12の多数枚の積層によりこの点
接触部分が到る所で生じ、水がまんべんなく行きわたり
水膜が形成されることになる。第5図では黒点は2枚の
板状体12 a、 12 bの接触部分のみを示してい
るが、上側の板状体の更シζ手前の板状体(図示省略)
及び下側の板状体の更に奥の板状体(図示省略)との間
の接触部分は更に多くなる。なお、空気流によって片方
の分流が他方より少な目となるので、垂直方向に対する
傾斜角度をずらした方が良い。
As a result, when water is sprinkled from the corrugated cross-section side, when the water flows down the front and back sides of the plate-shaped body 12, the water branches and flows at the point contact area, and the stacking of many plates of the plate-shaped body 12 causes the water to flow down the front and back sides of the plate-shaped body 12. Contact points occur everywhere, allowing water to spread evenly and forming a water film. In FIG. 5, the black dots show only the contact parts of the two plate-shaped bodies 12a and 12b, but the plate-shaped body (not shown) in front of the upper plate-shaped body is removed.
The number of contact areas between the lower plate-shaped body and the deeper plate-shaped body (not shown) increases further. Note that since one branched flow will be smaller than the other depending on the airflow, it is better to shift the inclination angle with respect to the vertical direction.

すなわち、第5図での右下り板状体12aよりも左下り
板状体12bの傾斜角度を急にすれば左側からの空気流
に対し水の分流量を同等にできる。
That is, by making the inclination angle of the left descending plate member 12b steeper than that of the right descending plate member 12a in FIG. 5, the amount of water diverted can be made equal to the air flow from the left side.

板状体12の材質は、親水性の表面を有するものが望ま
しく、グラスファイバを骨材とした複合セラミックス薄
板等が好ましいが、一般空調用に使用する場合には、耐
水強度のあるセルローズ繊維を主体とした耐水紙の如き
ものでもよい。いずれにしても、保持水量と空気流の風
圧に副える湿り強度を有するものが必要である。また、
空気流路の動水径は実験上8m以上がスケールの成長防
止、空気流の貫流損失を小さくするため有効である。
The material of the plate-shaped body 12 is preferably one with a hydrophilic surface, such as a composite ceramic thin plate made of glass fiber as an aggregate, but when used for general air conditioning, cellulose fiber with water resistance is preferable. A material such as waterproof paper may be used as the main material. In any case, it is necessary to have a wet strength that can support the amount of water it can hold and the wind pressure of the air flow. Also,
Experimentally, it has been found that the hydraulic diameter of the air flow path is 8 m or more, which is effective in preventing scale growth and reducing the through-flow loss of the air flow.

第6図は長手凹溝12cの壁に当って通過する空気流の
流れを示している。この図の如く長手凹溝12cを形成
する波形の壁は空気流の壁ともなり空気流は水膜に衝突
する。そして、この衝突によってダストの吸着やガス、
臭気の吸収が行なわれる。
FIG. 6 shows the flow of air that hits the wall of the longitudinal groove 12c and passes through it. As shown in this figure, the corrugated wall forming the longitudinal groove 12c also serves as a wall for airflow, and the airflow collides with the water film. This collision causes adsorption of dust, gas,
Absorption of odors takes place.

空気流は、加熱や冷却と近似する回速3 m/see位
のものを使用すれば、使いやすく、エレメントの厚さを
200m位にすると接触係数は80%以上になるにもか
かわらず、静圧損失が7 m Aq At下にできる。
Air flow is easy to use if you use a rotational speed of about 3 m/see, which is similar to heating and cooling, and when the element thickness is about 200 m, the contact coefficient becomes over 80%, but it is still static. The pressure loss is below 7 mAq At.

なお、この場合、水の重量速度/空気の重量速度(L/
G)は0.01〜0.4位の値が良く、これを大きめに
とると温水使用では加熱・加湿効果が得られ、冷水を使
用すれば冷却・除湿効果が得られる。
In this case, the weight velocity of water/weight velocity of air (L/
A value of about 0.01 to 0.4 is good for G), and if it is set to a large value, heating and humidifying effects can be obtained when hot water is used, and cooling and dehumidifying effects can be obtained when cold water is used.

第7図は本実施例装置を集塵装置として用いた場合の面
風速に対するms+効率を示したものであり、JIS8
種類規格のダストにて面風速を上昇させても集塵効率は
さほど低下しないもので、例えば1.5m/gの面風速
で80%の集塵効率であるとき3m/seeの面風速と
しても40%まで低下せず70%の集塵効率を保持する
Figure 7 shows the ms+efficiency with respect to the surface wind speed when the device of this embodiment is used as a dust collector, and is based on JIS8
Even if the surface wind speed is increased with type-standard dust, the dust collection efficiency will not decrease much. For example, if the surface wind speed is 80% at a surface wind speed of 1.5 m/g, even if the surface wind speed is 3 m/see. Maintains dust collection efficiency of 70% without decreasing to 40%.

しかもこの場合、従来技術にて述べた一般のフィルタの
如く清掃は必要なく水の流下によってダストも流され常
に洗浄していると同等の効果を有する。したがって、空
調用のみならずペイントミスト、オイルミストを含む産
業空気処理用として有効である。
Moreover, in this case, unlike the general filter described in the prior art, cleaning is not necessary, and the dust is also washed away by the flowing water, so that the same effect can be obtained as if the filter were constantly cleaned. Therefore, it is effective not only for air conditioning but also for industrial air treatment including paint mist and oil mist.

また、用途上高性能フィルタをメインフィルタとして使
用する場合、そのプレフィルタとして本実施例フィルタ
を使用すれば水滴が発生しないので、水滴飛散によりメ
インフィルタを濡らすことがなく、白粉の発生やバクテ
リアの発生の心配がない。
In addition, when a high-performance filter is used as the main filter for the purpose of application, if this example filter is used as a pre-filter, water droplets will not be generated, so the main filter will not be wetted by flying water droplets, and white powder and bacteria will not be generated. There is no need to worry about it occurring.

また、従来のウォーターカーテンと異なり衝突捕集が繰
返し行なわれることになり、捕集率が高い。
Furthermore, unlike conventional water curtains, collision collection is performed repeatedly, resulting in a high collection rate.

本実施例では、本漬捕集でないのでエアワッシャーより
高効率で水滴の再飛散もない。
In this example, since the actual collection is not carried out, the efficiency is higher than that of an air washer, and there is no re-scattering of water droplets.

本実施例装置を脱ガス・脱臭装置とした場合、空気の衝
突捕集によるため高補集率で浄化できるのであるが、こ
れは排水の分析により計算できるのであるが、特に有害
なガスや臭気が水と親和性を有する場合、水の吸収浄化
機能が加算されるためその効率は著しく高くなる。また
、原因物質は排水中に1lltaされているため、その
処理は容易で、特別な薬剤を使用しないので二次公害の
おそれもない。
When the device of this embodiment is used as a degassing/deodorizing device, it can be purified with a high collection rate due to air collision collection, which can be calculated by analyzing wastewater, but especially harmful gases and odors can be purified. When it has an affinity for water, its efficiency becomes significantly higher because it has an additional function of absorbing and purifying water. In addition, since the causative substance is contained in the wastewater, its treatment is easy, and since no special chemicals are used, there is no risk of secondary pollution.

浮遊微生物の捕集に当っては、水滴によらず水膜による
ため再飛散の現象がなく、効果的である。しかも、水滴
の再飛散の防止は給水中のバクテリアが蒸発により更に
加わるというような問題もなくなる。
When collecting floating microorganisms, it is effective because there is no re-scattering phenomenon because it uses a water film instead of water droplets. Moreover, prevention of re-scattering of water droplets also eliminates the problem of bacteria in the water supply being added due to evaporation.

循環水を使用する場合も時間当り換水率を時間当りの微
生物増殖率より大きくすれば、処理水中の微生物量を安
全な値にコントロールすることができる。
Even when circulating water is used, the amount of microorganisms in the treated water can be controlled to a safe value by making the water change rate per hour higher than the microbial growth rate per hour.

また、加湿器としては、本実施例では水滴の発生がなく
、水腹による蒸発のみ行なわれるので、白粉現象も全く
起らず加湿吸収距離も必要なくて装置全体がコンパクト
であし、スケールの成長も給水の水質によって余剰水車
を決めておけば水中の各イオン濃度がコントロールでき
る。
In addition, as a humidifier, in this embodiment, water droplets are not generated, and only evaporation is performed by the water belly, so no white powder phenomenon occurs, no humidification absorption distance is required, the entire device is compact, and scale growth is reduced. However, by determining the surplus water wheel depending on the quality of the water supply, the concentration of each ion in the water can be controlled.

更に、冷却器としては、板状体表面の水膜から水が気化
して、気化潜熱を奪うので冷却効果が発揮される。
Furthermore, as a cooler, water evaporates from the water film on the surface of the plate-like body and takes away the latent heat of vaporization, so that a cooling effect is exhibited.

すなわち、たとえば中間期外気冷房を行なう場合、特に
近代ビルでは断熱性と気密性が高いので冬季でも外気冷
房の必要があるが、これを効果的に行なうことができる
。また、夏季には空調用冷却器として一般的に冷房を行
なうが、本実施例を冷却器として空調器前段に使用して
も、冷却と共に加湿が生じ、湿り空気線図上では等湿球
線に沿って冷却が起るためエネルギー的には節約となら
ない。ところが、冷却器の入口空気の湿度が上昇しても
エンタルピは上昇せず、冷却器への負荷が上昇すること
がない。よって、ダストや微生物によって汚染しゃすい
湿り冷却器の前段で自浄作用を有するプレフィルタを設
置したことになり、質の良い空調が行なえる。
That is, for example, when performing outside air cooling during a mid-term period, especially in modern buildings, which have high insulation and airtightness, outside air cooling is necessary even in winter, and this can be done effectively. In addition, in the summer, air conditioning coolers are generally used for cooling, but even if this example is used as a cooler in the front stage of an air conditioner, humidification will occur along with cooling, and the isohumidity bulb line will appear on the psychrometric diagram. Since cooling occurs along the line, there is no energy saving. However, even if the humidity of the inlet air of the cooler increases, the enthalpy does not increase, and the load on the cooler does not increase. Therefore, a self-cleaning pre-filter is installed upstream of the moisture cooler, which is susceptible to contamination with dust and microorganisms, and high-quality air conditioning can be achieved.

その低木実施例では、可動部分がなく、エネルギを消費
せず、騒音もなく寿命が長く、保守容易、耐火性、小型
、静圧損失がわずかである。
Its shrub embodiment has no moving parts, consumes no energy, is noiseless, has a long lifespan, is easy to maintain, fire resistant, small size, and has low static pressure losses.

〈発明の効果〉 以上説明したように本発明では、水滴でなく水膜により
ダストの捕集、ガス臭気の吸収、微生物の捕集ができ、
かつ水の流下を伴うため洗浄作用が生じて、衝突捕集効
率を上昇でき、加湿器、冷却器としても極めて有用であ
る。
<Effects of the Invention> As explained above, in the present invention, dust can be collected, gas odors can be absorbed, and microorganisms can be collected using a water film instead of water droplets.
In addition, since water flows down, a cleaning action occurs and the collision collection efficiency can be increased, making it extremely useful as a humidifier and a cooler.

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

第1図ないし第7図は本発明の実施例で、第1図は空気
処理装置の一例の構成図、第2図はエレメントの一部切
欠構成図、第3図は板状体の分解斜視図、第4図は積層
状態図、第5図は板状体の点接触の説明図、第6図は空
気流通状態図、第7図は集塵効率に対する面風速の線図
である。 図  中、 11は空気処理装置、 12、12 a、 12 bは板状体、13は放出管、 14は水槽、 15は供給管、 16.20はバルブ、 17はポンプ、 12cは長手凹溝である。 第1図 3
Figures 1 to 7 show embodiments of the present invention, where Figure 1 is a configuration diagram of an example of an air treatment device, Figure 2 is a partially cutaway configuration diagram of an element, and Figure 3 is an exploded perspective view of a plate-shaped body. 4 is a stacking state diagram, FIG. 5 is an explanatory diagram of point contact of plate-like bodies, FIG. 6 is an air circulation state diagram, and FIG. 7 is a diagram of surface wind speed versus dust collection efficiency. In the figure, 11 is an air treatment device, 12, 12a, 12b are plates, 13 is a discharge pipe, 14 is a water tank, 15 is a supply pipe, 16.20 is a valve, 17 is a pump, and 12c is a longitudinal groove. It is. Figure 1 3

Claims (2)

【特許請求の範囲】[Claims] (1)山谷が交互に連続する断面を有しかつこの山谷に
よって表側及び裏側より長手凹溝が形成される板状体を
、多数枚その厚さ方向に積層すると共に隣接する上記板
状体の上記長手凹溝をある角度有して交互に積層し、相
互に隣接する一方の板状体の上記長手凹溝を形成する谷
の底部と他方の板状体の上記長手凹溝を形成する山の頂
部とを点接触させた空気処理エレメント。
(1) A large number of plate-like bodies having cross-sections in which peaks and valleys are continuous and longitudinal grooves are formed from the front and back sides by the peaks and valleys are stacked in the thickness direction, and the adjacent plate-like bodies are stacked together in the thickness direction. The longitudinal grooves are stacked alternately at a certain angle, with the bottoms of the valleys forming the longitudinal grooves of one plate-shaped body and the ridges forming the longitudinal grooves of the other plate-shaped body adjacent to each other. air treatment element in point contact with the top of the air treatment element.
(2)表裏に長手凹溝を形成する板状体を厚さ方向に積
層して構成される空気処理エレメントを上記長手凹溝が
上下に立つように上面に山谷が交互に連続する断面を臨
ませ、この上面上方に散水装置を配置すると共に下面下
方に水受けである水槽を配置した水膜型空気処理装置。
(2) An air treatment element constructed by laminating plate-shaped bodies with longitudinal grooves on the front and back sides in the thickness direction is shown in cross section with alternating peaks and valleys on the top surface so that the longitudinal grooves stand up and down. This is a water film type air treatment device in which a water sprinkler is placed above the top surface and a water tank serving as a water receptacle is placed below the bottom surface.
JP2081191A 1990-03-30 1990-03-30 Air treating element and water screen-type air treating device having the same Pending JPH03284319A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2081191A JPH03284319A (en) 1990-03-30 1990-03-30 Air treating element and water screen-type air treating device having the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2081191A JPH03284319A (en) 1990-03-30 1990-03-30 Air treating element and water screen-type air treating device having the same

Publications (1)

Publication Number Publication Date
JPH03284319A true JPH03284319A (en) 1991-12-16

Family

ID=13739579

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2081191A Pending JPH03284319A (en) 1990-03-30 1990-03-30 Air treating element and water screen-type air treating device having the same

Country Status (1)

Country Link
JP (1) JPH03284319A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001527203A (en) * 1997-12-22 2001-12-25 マンタース アーベー Air treatment unit
JP2001355985A (en) * 2000-06-14 2001-12-26 Takasago Thermal Eng Co Ltd Heat transferring apparatus and substance transferring apparatus
JP2008093535A (en) * 2006-10-10 2008-04-24 Takasago Thermal Eng Co Ltd Obliquely corrugated material and gas-liquid contact filling
JP2009530097A (en) * 2006-03-21 2009-08-27 トランスバック・システムズ・リミテッド Matrix structure
JP2011247454A (en) * 2010-05-24 2011-12-08 Taikisha Ltd Air purification and humidification device
CN102908845A (en) * 2012-10-23 2013-02-06 温坚 Air purifier

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001527203A (en) * 1997-12-22 2001-12-25 マンタース アーベー Air treatment unit
US6409157B1 (en) * 1997-12-22 2002-06-25 Munters Ab Air treatment unit
JP2001355985A (en) * 2000-06-14 2001-12-26 Takasago Thermal Eng Co Ltd Heat transferring apparatus and substance transferring apparatus
JP2009530097A (en) * 2006-03-21 2009-08-27 トランスバック・システムズ・リミテッド Matrix structure
JP2008093535A (en) * 2006-10-10 2008-04-24 Takasago Thermal Eng Co Ltd Obliquely corrugated material and gas-liquid contact filling
JP2011247454A (en) * 2010-05-24 2011-12-08 Taikisha Ltd Air purification and humidification device
CN102933910A (en) * 2010-05-24 2013-02-13 株式会社大气社 Air purifier and humidifier
CN102933910B (en) * 2010-05-24 2015-11-25 株式会社大气社 Air-purifying humidification device
CN102908845A (en) * 2012-10-23 2013-02-06 温坚 Air purifier

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