JP2003222363A - Air cleaning method - Google Patents

Air cleaning method

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Publication number
JP2003222363A
JP2003222363A JP2002024290A JP2002024290A JP2003222363A JP 2003222363 A JP2003222363 A JP 2003222363A JP 2002024290 A JP2002024290 A JP 2002024290A JP 2002024290 A JP2002024290 A JP 2002024290A JP 2003222363 A JP2003222363 A JP 2003222363A
Authority
JP
Japan
Prior art keywords
air
water
metal
honeycomb
chemical
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2002024290A
Other languages
Japanese (ja)
Other versions
JP3716926B2 (en
Inventor
Isao Terada
功 寺田
Satoshi Minobe
智 美濃部
Toshihisa Okabe
稔久 岡部
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.)
Nichias Corp
Original Assignee
Nichias Corp
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 Nichias Corp filed Critical Nichias Corp
Priority to JP2002024290A priority Critical patent/JP3716926B2/en
Publication of JP2003222363A publication Critical patent/JP2003222363A/en
Application granted granted Critical
Publication of JP3716926B2 publication Critical patent/JP3716926B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Gas Separation By Absorption (AREA)
  • Air Humidification (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an air processing method having a high removal efficiency for gaseous chemical contaminants in the air, using a compact processing device, with small pressure loss, and low cost. <P>SOLUTION: This air cleaning method comprises a humidifying step for humidifying, by a humidifying means 13, the air containing the chemical contaminants and taking a part of the gaseous contaminants in the air into excess moisture for removal from the air; and a dehumidifying step for dehumidifying the humidified air by a condensing means 23 and taking the gaseous chemical contaminants remaining without being removed in the humidifying step into condensate for removal. Air is led from the front opening part of a honeycomb 1 by using the metal oblique honeycomb 1 having opened both front and rear faces and upper and lower faces disposed on one or both of the humidifying means 13 and the condensing means 23, and water is supplied from the front opening part. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、空気中の化学汚染
物質を水で洗浄して清浄にする空気清浄方法に関するも
のである。さらに詳しくは、半導体や液晶デバイスの製
造工場、製薬工場やライフサイエンス関連設備等のクリ
ーンルームに供給する空気の空気清浄方法に関するもの
である。
TECHNICAL FIELD The present invention relates to an air cleaning method for cleaning chemical pollutants in the air with water. More specifically, the present invention relates to an air cleaning method for air supplied to a clean room such as a semiconductor or liquid crystal device manufacturing factory, a pharmaceutical factory or a life science-related facility.

【0002】[0002]

【従来の技術】半導体や液晶デバイスの製造工場、製薬
工場やライフサイエンス関連設備等では、製品歩留りを
向上し、或いは品質確保するために、従来の微粒子状の
汚染物質に加え、ガス状化学汚染物質をも除去すること
が望まれている。このような化学汚染物質としては、例
えば、ナトリウム、カリウム、カルシウム、ホウ素等の
無機質の金属元素、フッ素イオン、塩化物イオン、硝酸
イオン、亜硝酸イオン、硫酸イオン、亜硫酸イオン等の
アニオン類やアンモニウムイオン等のカチオン類等が挙
げられる。従来の微粒子状の汚染物質は、ULPAフィ
ルター等の集塵フィルターで除去できるが、これらの化
学汚染物質は、ULPAフィルター等では除去できな
い。
2. Description of the Related Art In semiconductor and liquid crystal device manufacturing factories, pharmaceutical factories, life science related facilities, etc., in order to improve product yield or ensure quality, in addition to conventional particulate contaminants, gaseous chemical contamination It is also desired to remove the substance. Examples of such chemical pollutants include inorganic metal elements such as sodium, potassium, calcium, and boron, anions such as fluorine ion, chloride ion, nitrate ion, nitrite ion, sulfate ion, and sulfite ion, and ammonium. Examples thereof include cations such as ions. Conventional particulate contaminants can be removed with a dust collecting filter such as a ULPA filter, but these chemical contaminants cannot be removed with a ULPA filter or the like.

【0003】このため、空気中の化学汚染物質は、従来
より、所謂、水シャワーと呼ばれる水滴のシャワーを用
いる方法や化学成分を吸着除去できるケミカルフィルタ
ーを用いる方法により除去される。ここで、前者の水シ
ャワーを用いる方法は、化学汚染物質を含む空気を水滴
の噴霧により取り除く方法である。
For this reason, chemical pollutants in the air are conventionally removed by a so-called water shower method using a shower of water droplets or a chemical filter capable of adsorbing and removing chemical components. Here, the former method of using a water shower is a method of removing air containing chemical contaminants by spraying water droplets.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、前者の
水シャワーを用いた方法は、被処理空気と水との接触効
率が悪いために化学汚染物質の除去効率が低い。このた
め、水シャワー装置からなる加湿手段の奥行きは数m程
度も必要となり、広大な設置スペースを要すると共に、
圧力損失も大きくなるという問題があった。また、水シ
ャワーの処理水としては、通常高価な脱イオン水(DI
W)が用いられているが、処理水量も多く必要となるた
めコストが高くなるという問題があった。さらに、低コ
スト化のためにDIWは、通常循環使用されているが、
一旦吸収した化学汚染物質の再気散が生じ易いという問
題があった。一方、後者のケミカルフィルターを用いた
方法は、ケミカルフィルター自体が高価であり、しかも
吸着能力に寿命があるため、コストが高くなるという問
題があった。
However, the former method using a water shower has a low efficiency of removing chemical pollutants because the contact efficiency between the air to be treated and water is poor. For this reason, the depth of the humidifying means composed of the water shower device is required to be several meters, which requires a vast installation space.
There was a problem that the pressure loss also increased. In addition, as the treated water for the water shower, usually expensive deionized water (DI
Although W) is used, there is a problem that the cost increases because a large amount of treated water is required. Furthermore, in order to reduce the cost, DIW is usually used in circulation,
There is a problem that the chemical pollutants once absorbed are likely to re-evaporate. On the other hand, the latter method using a chemical filter has a problem in that the cost is high because the chemical filter itself is expensive and the adsorption capacity has a life.

【0005】従って、本発明の目的は、空気中の化学汚
染物質の除去効率が高く、処理装置がコンパクトで、圧
力損失が小さく、低コストな空気清浄方法を提供するこ
とにある。
Therefore, it is an object of the present invention to provide an air cleaning method which has a high efficiency of removing chemical pollutants in the air, a compact processing apparatus, a small pressure loss, and a low cost.

【0006】[0006]

【課題を解決するための手段】かかる実情において、本
発明者らは鋭意検討を行った結果、加湿手段又は凝縮手
段の一方又は両方に、金属製斜行ハニカムを用い、該金
属製斜行ハニカムの前面開口部から空気を導入すると共
に、上面開口部から水を供給すれば、金属製斜行ハニカ
ムに導入される空気と供給される水とが効率よく接触し
て、加湿手段においては効率よく空気中の湿度を上昇さ
せることができる。また、凝縮手段においては、ガス状
化学汚染物質が凝縮水中に効率よく取り込まれて除去さ
れることを見出し、本発明を完成するに至った。
Under such circumstances, as a result of intensive investigations by the present inventors, a metal oblique honeycomb was used for one or both of the humidifying means and the condensing means, and the metal oblique honeycomb was used. If the air is introduced from the front opening of the and the water is supplied from the upper opening, the air introduced into the metal oblique honeycomb and the supplied water efficiently contact each other, and the humidifying means efficiently. The humidity in the air can be increased. Further, in the condensing means, it was found that the gaseous chemical pollutants were efficiently taken in and removed from the condensed water, and the present invention was completed.

【0007】すなわち、本発明の請求項1記載の発明
は、前後両面と上下両面とが開口して配置された金属製
斜行ハニカムの前面開口部から化学汚染物質を含む空気
を導入すると共に、上面開口部から水を供給すること
で、前記空気を加湿させ、得られる過剰な水分に化学汚
染物質の少なくとも一部を取り込むことで、空気中から
化学汚染物質を除去することを特徴としている。
That is, according to the first aspect of the present invention, air containing chemical pollutants is introduced from the front opening of a metal oblique honeycomb having front and rear surfaces and upper and lower surfaces opened. It is characterized in that the air is humidified by supplying water from the upper surface opening, and at least a part of the chemical pollutants is taken into the excess water obtained, thereby removing the chemical pollutants from the air.

【0008】本発明の請求項2記載の発明は、前後両面
と上下両面とが開口して配置された金属製斜行ハニカム
の前面開口部から化学汚染物質を含む空気を導入すると
共に、上面開口部から水を供給することで、前記空気を
除湿させ、得られる凝縮水に化学汚染物質の少なくとも
一部を取り込むことで、空気中から化学汚染物質を除去
することを特徴としている。
According to a second aspect of the present invention, air containing chemical pollutants is introduced from the front opening of a metal oblique honeycomb in which both front and rear surfaces and upper and lower surfaces are opened, and at the same time, an upper surface opening is provided. It is characterized in that the air is dehumidified by supplying water from the section, and at least a part of the chemical pollutants is taken into the obtained condensed water to remove the chemical pollutants from the air.

【0009】本発明の請求項3記載の発明は、化学汚染
物質を含む空気を導入すると共に、該空気と水とを接触
することで、前記空気を加湿させ、得られる過剰な水分
に化学汚染物質の少なくとも一部を取り込むことで、空
気中から化学汚染物質を除去する加湿工程と、化学汚染
物質を含む空気を導入させ、該空気と水とを接触するこ
とで、前記空気を除湿し、得られる凝縮水に化学汚染物
質の少なくとも一部を取り込むことで、空気中から化学
汚染物質を除去する除湿工程とを有する空気洗浄方法で
あって、加湿工程で使用する加湿手段、及び除湿手段で
使用する凝縮手段として、前後両面と上下両面とが開口
して配置された金属製斜行ハニカムを前記両手段の一方
又は両方に使用することを特徴としている。
According to a third aspect of the present invention, the air containing chemical pollutants is introduced, and the air and water are contacted to humidify the air. By incorporating at least a part of the substance, a humidification step of removing chemical pollutants from the air, and introducing air containing chemical pollutants, by contacting the air and water, dehumidifying the air, An air cleaning method having a dehumidifying step of removing chemical pollutants from the air by incorporating at least a part of the chemical pollutants in the obtained condensed water, the humidifying means used in the humidifying step, and the dehumidifying means. As the condensing means to be used, a diagonal metal honeycomb having front and rear surfaces and upper and lower surfaces opened is used for one or both of the both means.

【0010】本発明の請求項4記載の発明は、前後両面
と上下両面とが開口して配置された金属製斜行ハニカム
の前面開口部から化学汚染物質を含む空気を導入すると
共に、上面開口部から水を供給し、前記金属製斜行ハニ
カムの前段部で該空気を加湿させ、得られる過剰な水分
に化学汚染物質の少なくとも一部を取り込むことで、空
気中から化学汚染物質を除去し、次いで前記空気を除湿
させ、得られる凝縮水に化学汚染物質の少なくとも一部
を取り込むことで、空気中から化学汚染物質を除去する
ことを特徴としている。
According to a fourth aspect of the present invention, air containing chemical pollutants is introduced from the front opening of a metal oblique honeycomb having front and rear surfaces and upper and lower surfaces opened, and an upper surface opening. From the air, the air is humidified in the front part of the oblique metal honeycomb, and at least a part of the chemical pollutants is taken into the excess water obtained, thereby removing the chemical pollutants from the air. Then, the air is dehumidified, and at least a part of the chemical pollutants is taken into the resulting condensed water to remove the chemical pollutants from the air.

【0011】[0011]

【発明の実施の形態】本発明において、加湿手段とは、
被処理空気への水分の供給手段及び適宜、水分の回収手
段や温度調整手段を備えることにより、被処理空気を所
定の湿度まで加湿すると共に、過剰な水分を得る手段で
ある。該加湿手段は、被処理空気を加湿すると共に、被
処理空気中に含まれるガス状化学汚染物質の少なくとも
一部を該余分な水分中に取り込んで除去するものであ
る。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, the humidifying means means
By providing a means for supplying moisture to the air to be treated and a means for collecting the moisture and a temperature adjusting means as appropriate, the means for humidifying the air to be treated to a predetermined humidity and obtaining excess moisture. The humidifying means humidifies the air to be treated and removes at least a part of the gaseous chemical contaminants contained in the air to be treated into the excess water.

【0012】凝縮手段とは、被処理空気と接触可能な低
温部及び水分の回収手段を備えることにより、被処理空
気を所定の湿度まで除湿すると共に、除湿の際に生じた
凝縮水を得る手段である。該凝縮手段は、被処理空気中
の化学汚染物質又は前記加湿手段で除去されなかった化
学汚染物質を除湿の際に生じる凝縮水に可能な限り取り
込んで除去するものである。
The condensing means is provided with a low temperature part which can come into contact with the air to be treated and a means for collecting water, so as to dehumidify the air to be treated to a predetermined humidity and obtain condensed water generated during dehumidification. Is. The condensing means removes the chemical pollutants in the air to be treated or the chemical pollutants not removed by the humidifying means by incorporating them into condensed water generated during dehumidification as much as possible.

【0013】本発明において、化学汚染物質としては、
高性能(ULPA)フィルターの編み目を通過するよう
な微細な化学物質を意味し、例えば、ナトリウム、カリ
ウム、カルシウム、ホウ素等の無機質の金属元素、フッ
素イオン、塩化物イオン、硝酸イオン、亜硝酸イオン、
硫酸イオン、亜硫酸イオン等のアニオン類やアンモニウ
ムイオン等のカチオン類等が挙げられる。
In the present invention, the chemical pollutants include
It means a fine chemical substance that passes through the stitches of a high performance (ULPA) filter. For example, inorganic metal elements such as sodium, potassium, calcium, and boron, fluoride ions, chloride ions, nitrate ions, nitrite ions. ,
Examples thereof include anions such as sulfate ion and sulfite ion and cations such as ammonium ion.

【0014】本発明では、上記加湿手段又は凝縮手段の
一方又は両方に、前後両面と上下両面とが開口した配置
された金属製斜行ハニカムを用いる。該金属製斜行ハニ
カムを図1を参照して説明する。ここで、金属製斜行ハ
ニカム1とは、一方向に向かって伝播する波形形状を有
する金属製波形シート2,3(以下、「金属製コルゲー
ト状シート」ともいう)が複数積層されてハニカム形状
を呈するものであって、積層される金属製コルゲート状
シート2,3は、波の伝播方向が一枚おきに斜めに交差
するように積層され、且つ、二層おきのシートの波の伝
播方向がそれぞれ略同一方向になるように配置されたハ
ニカム状体である。
In the present invention, one or both of the humidifying means and the condensing means use a metal oblique honeycomb in which both front and rear surfaces and upper and lower surfaces are open. The metal oblique honeycomb will be described with reference to FIG. Here, the metal oblique honeycomb 1 is a honeycomb shape in which a plurality of metal corrugated sheets 2 and 3 (hereinafter, also referred to as “metal corrugated sheet”) having a corrugated shape that propagates in one direction are stacked. The metal corrugated sheets 2 and 3 to be laminated are laminated so that the wave propagation directions of every other sheet diagonally intersect, and the wave propagation direction of every two layers. Are honeycomb-shaped bodies arranged so as to be substantially in the same direction.

【0015】該金属製斜行ハニカム1は、金属製コルゲ
ート状シート2,3に平行な面に対して垂直な4面10
1〜104で切断して直方体を形成し、該切断面が金属
製コルゲート状シート2,3の波の伝播方向と平行でな
く、且つ、垂直でもないようにした場合、該直方体を切
断面の1つ104を下面にし、金属製コルゲート状シー
ト2,3の最外層105,106をそれぞれ左右面にし
て載置すると、切断面である前後両面102,103及
び上下両面101,104の4面は、全てハニカムセル
が開口し、左右面105,106は金属製コルゲート状
シート2,3で閉じられた構造を有するものである。ま
た、該切断面の、例えば、前後両面102,103は、
斜め上方向に延設されるセルと斜め下方向に延設される
セルとが一層おきに形成される。斜め上方向に延設され
るセルの前後両面から見た場合の空気の流入、流出方向
(水平方向)に対する斜め角度(図中、符号X)は、通
常15〜45度、好ましくは25〜35度の範囲内にす
る。上記斜め角度が該範囲内にあると、流下速度が適度
の範囲となり接触効率が向上するため好ましい。
The metal oblique honeycomb 1 has four surfaces 10 which are perpendicular to the surfaces parallel to the metal corrugated sheets 2 and 3.
1 to 104 is cut to form a rectangular parallelepiped, and the cut surface is not parallel to the wave propagation direction of the metal corrugated sheets 2 and 3 and is not perpendicular to the rectangular parallelepiped. When one is placed on the lower side and the outermost layers 105 and 106 of the metal corrugated sheets 2 and 3 are placed on the left and right sides, respectively, the four front and back sides 102 and 103 and the four upper and lower sides 101 and 104, which are cut surfaces, The honeycomb cells are all opened, and the left and right surfaces 105 and 106 are closed by the metal corrugated sheets 2 and 3. Further, for example, the front and rear surfaces 102 and 103 of the cut surface are
The cells extending diagonally upward and the cells extending diagonally downward are formed alternately. The oblique angle (reference numeral X in the figure) with respect to the inflow / outflow direction (horizontal direction) of air when viewed from the front and rear surfaces of the cell extending obliquely upward is usually 15 to 45 degrees, preferably 25 to 35. Within the range of degrees. It is preferable that the above-mentioned oblique angle is within this range, because the flow-down velocity is in the appropriate range and the contact efficiency is improved.

【0016】上記金属製斜行ハニカム1において、積層
された金属製コルゲート状シート2,3の一層おきの波
の伝播方向が互いに交差する角度(図中、符号Y)は、
通常30〜90度、好ましくは25〜35度である。こ
のような金属製コルゲート状シート2,3を互いに上記
角度範囲内で交差するように積層すると、上記のように
斜め角度(X)を上記の15〜45度とした場合に、被
処理空気及び水がハニカムセルと実質的に接触する面積
が大きくなるため、被処理空気と水との接触、すなわ
ち、加湿手段においては被処理空気の加湿の効率、ま
た、凝縮手段においては、被処理空気中の水分の凝縮に
よる除湿の効率が高くなるため好ましい。つまり、後述
するように、本発明において、被処理空気は金属製斜行
ハニカム1の前面開口部103から導入され、水は上面
開口部101から例えば、給水ダクト4により供給され
金属製斜行ハニカム1の金属製コルゲート状シート2,
3に表面を下方に流下するため、被処理空気の通気方向
と浸透壁面の水の流下方向とが適度の角度を保持し、接
触効率が高くなる。
In the above-described metal diagonal honeycomb 1, the angle at which the wave propagating directions of the stacked metal corrugated sheets 2 and 3 alternate with each other (symbol Y in the figure) is
It is usually 30 to 90 degrees, preferably 25 to 35 degrees. When such metal corrugated sheets 2 and 3 are laminated so as to intersect with each other within the above angle range, the air to be treated and the air to be treated when the oblique angle (X) is set to 15 to 45 degrees as described above. Since the area where water substantially contacts the honeycomb cells becomes large, the contact between the air to be treated and the water, that is, the humidification efficiency of the air to be treated in the humidifying means, and the air to be treated in the condensing means This is preferable because the efficiency of dehumidification due to the condensation of the water content is increased. That is, as will be described later, in the present invention, the air to be treated is introduced from the front opening 103 of the metal oblique honeycomb 1, and the water is supplied from the top opening 101, for example, by the water supply duct 4, to the metal oblique honeycomb. 1 metal corrugated sheet 2,
3, the surface flows downward, so that the air flow direction of the air to be treated and the water flow direction of the permeation wall surface maintain an appropriate angle, and the contact efficiency becomes high.

【0017】本発明に用いられる金属製斜行ハニカム1
のセルの高さ、すなわち、波の山と谷間の寸法を示すセ
ルの山高寸法は、通常1.5〜8mm、好ましくは2.
0〜5mmである。セル寸法が1.5mm未満であると
製造が困難であり、圧力損失が大きくなるため好ましく
ない。また、セル寸法が8mmを越えると、ガス状化学
汚染物質の除去効率が低下するため好ましくない。
Metal oblique honeycomb 1 used in the present invention
The height of the cell, that is, the height of the peak of the cell indicating the size of the crests and troughs of the wave is usually 1.5 to 8 mm, preferably 2.
It is 0 to 5 mm. If the cell size is less than 1.5 mm, manufacturing is difficult and pressure loss increases, which is not preferable. Further, if the cell size exceeds 8 mm, the efficiency of removing gaseous chemical pollutants decreases, which is not preferable.

【0018】金属製斜行ハニカム1の金属製コルゲート
状シート2,3の状態におけるセルの幅、すなわち、セ
ルピッチは通常2.5〜12.0mm、好ましくは3.
0〜10.0mmである。また、金属製斜行ハニカム1
の前面開口部と後面開口部との間の寸法、すなわち、金
属製斜行ハニカム1の厚さ(t)は、特に制限されない
が、通常100〜1000mm、好ましくは200〜8
00mmである。また、梅雨時のように湿度が高い時期
に、1台のハニカムで化学汚染物質の除去と除湿とを行
う場合には、除湿を十分に行うために800mm程度の
厚いものを使用した方がよい。該厚さが100mm未満
であると、NO2 -等の除去効率が低下するため好ましく
なく、厚さが1000mmを越えると、化学汚染物質の
除去効率がこれ以上向上せず、圧力損失が大きくなるた
め好ましくない。なお、本発明において、金属製斜行ハ
ニカム1の厚さは、該金属製斜行ハニカム1を複数枚使
用する場合には、この合計の厚さが上記範囲内のもので
あればよい。例えば、厚さが300mmの金属製斜行ハ
ニカムを用いる場合には、厚さが100mmの金属製斜
行ハニカムを3枚厚さ方向に重ねて合計の厚さを300
mmとしてもよい。なお、従来加湿手段として用いられ
ていた水シャワーは、装置の奥行きが数m程度必要であ
るが、本発明に係る金属製斜行ハニカムを加湿手段とし
て用いると、金属製斜行ハニカム自体の厚さはせいぜい
400mm程度であるため、装置の設置スペースを大幅
に小さくすることができる。このような大幅な省スペー
ス化は半導体製造工場等の合理化の要求を満足する。さ
らに、水を循環するポンプの動力は、従来の水シャワー
のものと比較すると格段に少なく、大幅な省エネルギー
化をも図ることができる。
The width of the cells in the state of the metal corrugated sheets 2 and 3 of the oblique metal honeycomb 1, that is, the cell pitch is usually 2.5 to 12.0 mm, preferably 3.
It is 0 to 10.0 mm. Also, the metal diagonal honeycomb 1
The dimension between the front opening and the rear opening, that is, the thickness (t) of the metal oblique honeycomb 1 is not particularly limited, but is usually 100 to 1000 mm, preferably 200 to 8.
It is 00 mm. Further, in the case of removing chemical contaminants and dehumidifying with one honeycomb at a time of high humidity such as rainy season, it is preferable to use a thick one of about 800 mm in order to sufficiently dehumidify. . If the thickness is less than 100 mm, the removal efficiency of NO 2 − and the like is lowered, which is not preferable, and if the thickness exceeds 1000 mm, the removal efficiency of chemical pollutants is not further improved and the pressure loss increases. Therefore, it is not preferable. In the present invention, the thickness of the metallic skewed honeycomb 1 may be within the above range when a plurality of the metallic skewed honeycombs 1 are used. For example, when a metal skewed honeycomb having a thickness of 300 mm is used, three metal skewed honeycombs having a thickness of 100 mm are stacked in the thickness direction to give a total thickness of 300.
It may be mm. The water shower that has been conventionally used as a humidifying means requires a depth of about several meters in the apparatus. However, when the metal oblique honeycomb according to the present invention is used as the humidifying means, the thickness of the metal oblique honeycomb itself is increased. Since the size is at most about 400 mm, the installation space of the device can be significantly reduced. Such drastic space saving satisfies the demand for rationalization in semiconductor manufacturing factories and the like. Furthermore, the power of the pump that circulates the water is much less than that of the conventional water shower, and it is possible to achieve significant energy savings.

【0019】本発明で使用される金属製斜行ハニカムの
材質は強度、化学的安定性等が金属ハニカム担体に要求
される条件を満たすものであればよく、特に限定されな
いが、例えばステンレス、アルミニウム、銅等が挙げら
れる。厚さは10〜200μmで、10μmより薄いと
強度や加工性が悪く、200μmを超えると重い、しか
も圧力損失が大きいという問題がある。好ましい厚さ
は、30〜100μmである。
The material of the oblique metal honeycomb used in the present invention is not particularly limited as long as its strength, chemical stability and the like satisfy the requirements of the metal honeycomb carrier, and examples thereof include stainless steel and aluminum. , Copper and the like. The thickness is 10 to 200 μm. When it is thinner than 10 μm, strength and workability are poor, and when it exceeds 200 μm, it is heavy and pressure loss is large. The preferred thickness is 30-100 μm.

【0020】本発明で用いられる金属製コルゲート状シ
ート2,3は、平板状金属箔をコルゲート加工してなる
ものであり、金属箔の面内の一方向に波が進行するよう
に凹凸が形成されたものである。ここでコルゲート加工
とは、平板状物を波形状物に加工することを意味する。
The metal corrugated sheets 2 and 3 used in the present invention are formed by corrugating a flat metal foil, and have irregularities formed so that waves propagate in one direction in the plane of the metal foil. It was done. Here, corrugation processing means processing a plate-shaped material into a corrugated material.

【0021】金属製コルゲート状シート2,3に成形す
る方法としては、径方向に振幅する波形の凹凸が表面に
形成された複数の歯車間に平板状シートを通すような公
知のコルゲーターを用いる方法が挙げられる。得られた
金属製コルゲート状シート2,3から上記金属製斜行ハ
ニカム1を成形する方法としては、例えば、まず、上記
金属製コルゲート状シート2,3を縦100mm(成形
後の厚み寸法)×横300mm程度の矩形の裁断型に対
し、波の伝播方向が矩形型の一辺に対して15〜45度
になるように配置して裁断して矩形のコルゲート状シー
トを作製し、次いで、得られた矩形のコルゲート状シー
トを1枚おきの波の伝播方向が斜交するように配置し、
これらを積層する方法が挙げられる。なお、このように
して製造した場合、上記裁断型の縦の長さが金属製斜行
ハニカム1枚の厚さとなる。このため、例えば、加湿手
段や凝縮手段に必要な金属製斜行ハニカムの厚さ、すな
わち、金属製斜行ハニカムの前面開口部と後面開口部と
の間の寸法を300mmとする場合には、縦100mm
の裁断型で作製した厚さ100mmの金属製斜行ハニカ
ムを厚さ方向に3枚重ねて使用すればよい。
As a method of forming the metal corrugated sheets 2 and 3, a known corrugator is used in which a flat sheet is passed between a plurality of gears having undulating undulations having a radial amplitude. Is mentioned. As a method of molding the above-mentioned metal skewed honeycomb 1 from the obtained metal corrugated sheets 2 and 3, for example, first, above-mentioned metal corrugated sheets 2 and 3 are 100 mm in length (thickness dimension after molding) × A rectangular corrugated sheet is prepared by arranging a rectangular cutting die having a width of about 300 mm so that the wave propagation direction is 15 to 45 degrees with respect to one side of the rectangular die, and cutting the corrugated sheet. Arranged rectangular corrugated sheets so that the wave propagation directions of every other sheet intersect.
The method of laminating these is mentioned. When manufactured in this manner, the vertical length of the cutting die is the thickness of one metal oblique honeycomb. For this reason, for example, when the thickness of the metal oblique honeycomb required for the humidifying means and the condensing means, that is, when the dimension between the front opening and the rear opening of the metal oblique honeycomb is 300 mm, Length 100mm
It is advisable to use three 100-mm-thick metal oblique honeycombs manufactured by the cutting type in a stack in the thickness direction.

【0022】本発明において、上記金属製斜行ハニカム
が上記加湿手段又は上記凝縮手段の一方又は両方に用い
られる場合、金属製斜行ハニカムは前後両面と上下両面
とが開口するように配置される。金属製斜行ハニカムを
このように配置することにより、金属製斜行ハニカムの
前面開口部から被処理空気を導入すると共に、上面開口
部から水を供給することが可能になり、被処理空気と水
との接触が被処理空気の通気方向と水の流下方向とが直
交するようになる。このため、加湿手段又は凝縮手段と
して、金属製斜行ハニカムを用いると、被処理空気と水
との接触効率が従来の水シャワーを用いた加湿手段や冷
却器を用いた凝縮手段に比べて高くなり、被処理空気中
に含まれる化学汚染物質を効率よく除去することがで
き、装置の奥行きを大幅に小さくすることができる。
In the present invention, when the metal oblique honeycomb is used for one or both of the humidifying means and the condensing means, the metal oblique honeycomb is arranged so that both front and rear surfaces and upper and lower surfaces are open. . By arranging the metal diagonal honeycomb in this way, it becomes possible to introduce the air to be treated from the front opening of the metal diagonal honeycomb and to supply water from the upper opening, and The contact with water makes the aeration direction of the air to be treated and the flowing direction of the water orthogonal to each other. Therefore, when a metal oblique honeycomb is used as the humidifying means or the condensing means, the contact efficiency between the air to be treated and water is higher than that of the conventional humidifying means using a water shower or the condensing means using a cooler. Therefore, the chemical contaminants contained in the air to be treated can be efficiently removed, and the depth of the apparatus can be greatly reduced.

【0023】金属製斜行ハニカムが加湿手段又は凝縮手
段に用いられる場合、該金属製斜行ハニカムを用いた具
体的な加湿手段又は凝縮手段としては、例えば、前後両
面と上下両面とが開口するように配置される金属製斜行
ハニカムと、該金属製斜行ハニカムの上面開口部から水
を供給する給水部と、金属製斜行ハニカムを流下した水
分を回収する水回収部と、給水部に供給する水の温度を
調節する加熱器又は熱交換機等とからなるものが挙げら
れる。流下した水分を回収しない場合、水回収部の代わ
りに、水放出部を設けてもよい。なお、金属製斜行ハニ
カムが加湿手段及び凝縮手段の両方に用いられる場合、
加湿手段及び凝縮手段の態様は同様であるが、除湿手段
に供給する水の水温を加湿手段に供給する水の水温より
も低くすればよい。加湿手段及び凝縮手段に供給する水
の水温は、適宜定めればよい。
When the diagonal metal honeycomb is used for the humidifying means or the condensing means, the specific humidifying means or condensing means using the metallic diagonal honeycomb is, for example, both front and rear surfaces and upper and lower surfaces are open. Diagonally arranged metal honeycomb, a water supply unit for supplying water from the upper surface opening of the metal oblique honeycomb, a water recovery unit for recovering water flowing down the metal oblique honeycomb, and a water supply unit And a heat exchanger or the like for adjusting the temperature of the water supplied to. When the water that has flowed down is not collected, a water discharge unit may be provided instead of the water collection unit. When the metal oblique honeycomb is used for both the humidifying means and the condensing means,
The humidifying means and the condensing means have the same aspect, but the water temperature of the water supplied to the dehumidifying means may be lower than the water temperature of the water supplied to the humidifying means. The water temperature of the water supplied to the humidifying means and the condensing means may be appropriately determined.

【0024】本発明において、金属製斜行ハニカムの使
用形態としては、具体的には、金属製斜行ハニカムが加
湿手段及び凝縮手段の両方に用いられる第1の実施形
態、金属製斜行ハニカムが加湿手段のみに用いられる第
2の実施形態、金属製斜行ハニカムが凝縮手段のみに用
いられる第3の実施形態、1台の金属製斜行ハニカムに
おいて、加湿手段と凝縮手段とを順次行う第4の実施形
態が挙げられる。
In the present invention, as a usage pattern of the metal oblique honeycomb, specifically, the first embodiment in which the metal oblique honeycomb is used as both the humidifying means and the condensing means, the metal oblique honeycomb is used. Is used only for the humidifying means, the third embodiment is used only for the condensing means using the metal oblique honeycomb, and the humidifying means and the condensing means are sequentially performed in one metal oblique honeycomb. A fourth embodiment can be mentioned.

【0025】第1の実施形態は、加湿手段及び凝縮手段
の両方に、水と被処理空気との接触効率のため金属製斜
行ハニカムを用いるため、最も化学汚染物質の除去効率
が高く、装置の設置面積及び使用水量が少なくて済み、
圧力損失が小さいため好ましい。また、加湿手段及び凝
縮手段の両方に供給する水としては、加湿手段及び凝縮
手段の両方共に、又は少なくとも凝縮手段に供給する水
は脱イオン水を用いると被処理空気の汚染が少ないため
好ましい。ただし、加湿手段と凝縮手段がそれぞれ独立
している場合には、加湿手段及び凝縮手段に供給する水
は、凝縮手段に供給される水の汚染がなるべく生じない
ように独立した系とすることで互いに混合しないように
することが好ましい。また、加湿手段に供給する水は、
市水又は工業用水を用いると低コスト化できるため好ま
しい。上記脱イオン水としては、特に制限されず、例え
ば、市水又は工業用水を前処理した後、イオン交換樹脂
で処理した処理水を用いることができる。
In the first embodiment, since the metal oblique honeycomb is used for both the humidifying means and the condensing means due to the contact efficiency between water and the air to be treated, the removal efficiency of the chemical pollutants is the highest and the apparatus The installation area and the amount of water used are small,
It is preferable because the pressure loss is small. As the water to be supplied to both the humidifying means and the condensing means, it is preferable to use deionized water as the water to be supplied to both the humidifying means and the condensing means, or at least to the condensing means because the air to be treated is less contaminated. However, when the humidifying means and the condensing means are independent of each other, the water supplied to the humidifying means and the condensing means should be an independent system so that the water supplied to the condensing means is not polluted as much as possible. It is preferable not to mix with each other. The water supplied to the humidifying means is
Use of city water or industrial water is preferable because the cost can be reduced. The deionized water is not particularly limited, and for example, city water or industrial water that has been pretreated and then treated with an ion exchange resin can be used.

【0026】次に、第1の実施形態における作用を説明
する。まず、被処理空気は、ダクトを通してブロアー等
により加湿工程に供される。加湿工程では、被処理空気
は、所定の温度に加温され、且つ、金属製斜行ハニカム
の上部から水が供給されて、該金属製斜行ハニカムをゆ
っくりと流下してセル全体が水膜壁構造になっている金
属製斜行ハニカムのセルの表面と接触する。この際、被
処理空気は膜面から蒸発する水分により加湿されると共
に、一方では被処理空気中の化学汚染物質の一部が水中
に吸収される。この結果、被処理空気から化学汚染物質
がある程度除去される。
Next, the operation of the first embodiment will be described. First, the air to be treated is supplied to a humidification step by a blower or the like through a duct. In the humidification step, the air to be treated is warmed to a predetermined temperature, and water is supplied from the upper part of the metal oblique honeycomb, and the metal oblique honeycomb is slowly flowed down so that the entire cell has a water film. It comes into contact with the surface of the cells of the diagonal metal honeycomb having a wall structure. At this time, the air to be treated is humidified by the water vaporized from the film surface, while at the same time, a part of the chemical pollutants in the air to be treated is absorbed in the water. As a result, some of the chemical contaminants are removed from the air to be treated.

【0027】加湿工程終了後、加湿された被処理空気は
凝縮工程に供給される。凝縮工程では、被処理空気は、
前記加湿工程よりも低温にされた金属製斜行ハニカムの
セルの表面で冷却されて空気中の水分が凝縮し、この際
に空気中に前記加湿工程で除去されずに残存する化学汚
染物質が略凝縮水に取り込まれ流下水と共に回収され、
被処理空気中から化学汚染物質が除去される。上記の加
湿工程における水の温度、及び凝縮工程における水の温
度、前者が後者よりも高いものであればよく、所望の湿
度又は温度の空気が得られるように、適宜調整すればよ
い。凝縮工程終了後は、そのまま、又は適宜湿度や温度
を調整してクリーンルーム等に用いられる清浄空気とし
て使用される。
After completion of the humidifying step, the humidified air to be treated is supplied to the condensing step. In the condensation process, the air to be treated is
The moisture in the air is condensed by being cooled on the surface of the cells of the metal oblique honeycomb that has been cooled to a temperature lower than that in the humidification step, and at this time, the chemical pollutants remaining in the air without being removed in the humidification step are It is almost taken into condensed water and collected along with the running water,
Chemical pollutants are removed from the air to be treated. The temperature of the water in the humidifying step and the temperature of the water in the condensing step, as long as the former is higher than the latter, may be appropriately adjusted so that air having a desired humidity or temperature can be obtained. After completion of the condensation step, the air is used as it is or as the clean air used in a clean room or the like by appropriately adjusting the humidity and the temperature.

【0028】なお、クリーンルーム内は、通常、温度が
23℃前後、相対湿度が40〜50%程度に調節される
ため、クリーンルーム用の浄化空気を調製する場合、加
湿工程及び凝縮工程の条件は、上記凝縮工程後に得られ
る浄化空気は、23℃前後に適宜加熱された際に上記範
囲内の相対湿度になるように設定される。この際に用い
られる加熱手段又は加湿手段としては特に限定されず、
電熱器や温水による加温器等の公知のものを用いること
ができる。このようにして得られた23℃前後、且つ、
相対湿度が40〜50%程度の浄化空気クリーンルーム
用空気として用いられる。
In the clean room, the temperature is usually adjusted to around 23 ° C. and the relative humidity is adjusted to about 40 to 50%. Therefore, when preparing purified air for the clean room, the conditions of the humidification step and the condensation step are as follows. Purified air obtained after the condensing step is set to have a relative humidity within the above range when appropriately heated to around 23 ° C. The heating means or humidifying means used at this time is not particularly limited,
Known devices such as an electric heater and a warm water heater can be used. Around 23 ° C. thus obtained, and
Used as purified air clean room air with relative humidity of about 40 to 50%.

【0029】本発明の第1の実施形態によれば、金属製
斜行ハニカムを構成する波形状の金属板表面を流下する
水で加湿又は凝縮するために、循環使用等により化学汚
染物質を含むようになった循環水を用いる場合でも、該
循環水から化学汚染物質が再気散することがほとんどな
い。すなわち、従来の方法では、汚染物質を含む水をシ
ャワー状で噴霧するため、ミストが空気に取り込まれて
化学汚染物質の再飛散を引き起こしていた。これに対し
て、本発明の方法では、表面積の大きなハニカム表面の
水のみが蒸発し、一度水に取り込まれた化学汚染物質
は、水側に残るので、汚染物質の再飛散は起こりにくい
と考えられる。このため、金属製斜行ハニカムを加湿手
段に用いる場合には、上記のように脱イオン水のみなら
ず市水や工業用水を用いることができる。また、化学汚
染物質の除去効率が高いため、公知の水シャワー等では
1〜2程度必要であった液ガス比を0.1程度とするこ
とができる。また、加湿工程や凝縮工程に用いられる水
を循環使用する場合に、使用する水量が少なくて済み、
この結果、ポンプ容量等が小さくて済む。
According to the first embodiment of the present invention, in order to humidify or condense the water flowing down the surface of the corrugated metal plate forming the oblique metal honeycomb with water, chemical pollutants are contained by recycling or the like. Even when using such circulating water, chemical pollutants rarely re-evaporate from the circulating water. That is, in the conventional method, since water containing pollutants is sprayed in the form of a shower, the mist is taken into the air and causes re-scattering of the chemical pollutants. On the other hand, in the method of the present invention, only the water on the surface of the honeycomb having a large surface area is evaporated, and the chemical pollutants once taken into the water remain on the water side, so that re-scattering of the pollutants is unlikely to occur To be Therefore, when the oblique metal honeycomb is used as the humidifying means, not only deionized water but also city water or industrial water can be used as described above. Further, since the removal efficiency of chemical contaminants is high, the liquid-gas ratio, which was required to be about 1 to 2 in the known water shower or the like, can be set to about 0.1. Also, when the water used in the humidification process and the condensation process is circulated, the amount of water used is small,
As a result, the pump capacity and the like can be small.

【0030】本発明の第2の実施形態は、加湿手段のみ
に、水と被処理空気との接触効率のため金属製斜行ハニ
カムを用いるものであり、従来公知の水シヤワー等の加
湿手段に比べて、第1の実施形態において、加湿手段に
金属製斜行ハニカムを用いた効果と同様の効果を奏する
ことができる。本例は、冬場の乾燥空気を被処理空気と
する場合に好適である。また、本例では、加湿手段のみ
で被処理空気中の化学汚染物質を除去できるが、凝縮手
段として、公知の冷却器を使用して、加湿後の空気を除
湿してもよい。
In the second embodiment of the present invention, a diagonal metal honeycomb is used only for the humidifying means because of the contact efficiency between water and the air to be treated. In comparison, in the first embodiment, it is possible to obtain the same effect as that of using the metal oblique honeycomb as the humidifying means. This example is suitable when dry air in winter is used as the air to be treated. Further, in this example, the chemical contaminants in the air to be treated can be removed only by the humidifying means, but a well-known cooler may be used as the condensing means to dehumidify the air after humidification.

【0031】本発明の第3の実施形態は、凝縮手段のみ
に、水と被処理空気との接触効率の良い金属製斜行ハニ
カムを用いるものであり、従来公知の冷却器等を用いる
凝縮手段に比べて、第1の実施形態において、凝縮手段
に金属製斜行ハニカム用いた効果と同様の効果を奏する
ことができる。また、この実施形態においては、凝縮手
段が金属製斜行ハニカムを用いており、被処理空気と水
との接触効率が高く、化学汚染物質の除去効率が高いた
め、凝縮手段のみでもある程度のガス状化学汚染物質の
除去が可能であり、加湿手段を設けずに設備に掛かるコ
ストを低減することができる。特に梅雨時から夏場にか
けては空気が高温高湿であり、そのまま被処理空気とし
て供給できるため、本実施の形態は特に有効である。本
例では、凝縮手段のみで被処理空気中の化学汚染物を除
去できるが、さらに、加湿手段として、公知の加湿器を
使用し、その後、上記金属製斜行ハニカムで除湿しても
よい。
The third embodiment of the present invention uses a diagonal metal honeycomb having a good contact efficiency between water and the air to be treated only as a condensing means, and a condensing means using a conventionally known cooler or the like is used. Compared with the above, in the first embodiment, it is possible to obtain the same effect as that of using the metal oblique honeycomb as the condensing means. Further, in this embodiment, the condensing means uses a metal diagonal honeycomb, the contact efficiency between the air to be treated and water is high, and the removal efficiency of chemical pollutants is high. The chemical contaminants can be removed, and the cost of equipment can be reduced without providing a humidifying means. In particular, the present embodiment is particularly effective because the air is hot and humid from the rainy season to the summer and can be directly supplied as the air to be treated. In this example, the chemical contaminants in the air to be treated can be removed only by the condensing means, but a known humidifier may be used as the humidifying means, and then dehumidification may be performed by the above-described metal oblique honeycomb.

【0032】本発明の第4の実施形態は、1台の金属製
斜行ハニカムにおいて、加湿工程と凝縮工程を順次行う
ものである。すなわち、被処理空気は、ダクトを通して
ブロアー等により金属製斜行ハニカムの前面の開口部に
供給される。金属製斜行ハニカムの前段側は加湿部とな
り、被処理空気は所定の湿度まで加湿され、該金属製斜
行ハニカム内で飽和状態にまで加湿されると、次いで、
通過する金属製斜行ハニカムの後段部では、所定の湿度
まで除湿されることとなる。このため、前記加湿部で該
空気中の化学汚染物質の一部が過剰な水分に取り込まれ
ると共に、前記除湿部により、前記加湿部で除去されず
に残存する化学汚染物質が凝縮水に取り込まれて除去さ
れる。
In the fourth embodiment of the present invention, a humidifying process and a condensing process are sequentially performed in one metal oblique honeycomb. That is, the air to be treated is supplied to the opening on the front surface of the oblique metal honeycomb through a duct or the like. The pre-stage side of the metal skewed honeycomb is a humidification section, the air to be treated is humidified to a predetermined humidity, and when it is humidified to a saturated state in the metal skewed honeycomb, then,
In the subsequent stage of the oblique metal-made honeycomb that passes through, it is dehumidified to a predetermined humidity. Therefore, a part of the chemical pollutants in the air is taken into the excess water in the humidification section, and the chemical pollutants remaining without being removed in the humidification section are taken into the condensed water by the dehumidification section. Be removed.

【0033】上記の本発明に係る空気清浄方法は、例え
ば、半導体や液晶デバイスの製造工場、製薬工場、ライ
フサイエンス関連施設等のクリーンルームに供給する空
気の空気清浄方法として用いることができる。また、特
に、半導体や液晶デバイスの製造工場において、当該方
法に使用される金属製斜行ハニカムの大きさは、例え
ば、縦1000〜5000mm、横1000〜5000
mm、厚さ100〜1000mmのものが使用できる。
The above-described air cleaning method according to the present invention can be used as an air cleaning method for air supplied to clean rooms such as semiconductor and liquid crystal device manufacturing factories, pharmaceutical factories, and life science related facilities. Further, in particular, in a semiconductor or liquid crystal device manufacturing factory, the size of the metal oblique honeycomb used in the method is, for example, 1000 to 5000 mm in length and 1000 to 5000 in width.
mm, thickness 100-1000 mm can be used.

【0034】[0034]

【実施例】次に、実施例を挙げて本発明をさらに具体的
に説明するが、本発明はこれに限定されるものではな
い。
EXAMPLES Next, the present invention will be described more specifically by way of examples, but the present invention is not limited thereto.

【0035】(実施例1〜10、比較例1〜3)表1〜
3に示す仕様の加湿手段及び凝縮手段を有する空気清浄
装置を作製し、これらをそれぞれ表4〜6に示す条件で
処理した結果、それぞれ表7〜9に示す結果が得られ
た。また、得られた浄化空気を表10〜12に示す条件
で加熱してクリーンルーム用の浄化空気を得た。結果を
表10〜12に示す。なお、実施例5〜9は、加湿ゾー
ンを設けずに被処理空気を直接に凝縮ゾーンに供給する
ものである。さらに、金属製斜行ハニカムは、表1〜3
に記載のSUS製コルゲート状シートが1層おきに交差
し、且つ、セルの斜め角度が空気の流入方向に対して3
0度であるものを用いた。また、加湿手段で用いられる
水と凝縮手段で用いられる水とはそれぞれ独立した系と
し、実施例4と比較例2については、それぞれの水は循
環使用し、実施例1〜3、5〜11及び比較例1、3に
ついては1パスとした。補給水は、循環水中の汚染物質
が所定濃度以下になるように供給した。例えば、循環水
中のアンモニアイオン濃度は、実施例3では100pp
b、実施例4では500ppbである。水中のアンモニ
アイオン濃度が500ppbを越えると、従来の水シャ
ワーではアンモニアの気散が起こり、その吸収除去率は
著しく低下する(比較例2)。表中、「エアオッシャ
ー」は水シャワーのことである。
(Examples 1 to 10, Comparative Examples 1 to 3) Tables 1 to 1
As a result of producing an air cleaning device having a humidifying means and a condensing means having specifications shown in Table 3 and treating these under the conditions shown in Tables 4 to 6, the results shown in Tables 7 to 9 were obtained. The purified air obtained was heated under the conditions shown in Tables 10 to 12 to obtain purified air for a clean room. The results are shown in Tables 10-12. In addition, in Examples 5 to 9, the air to be treated is directly supplied to the condensation zone without providing the humidification zone. Further, the oblique metal honeycombs are shown in Tables 1 to 3.
The corrugated sheet made of SUS described in 1. intersects with every other layer, and the diagonal angle of the cell is 3 with respect to the inflow direction of air.
The one with 0 degree was used. Further, the water used in the humidifying means and the water used in the condensing means are independent systems, and in Example 4 and Comparative Example 2, each water is circulated and used in Examples 1 to 3 and 5 to 11. Also, for Comparative Examples 1 and 3, 1 pass was set. Make-up water was supplied so that pollutants in the circulating water were below a predetermined concentration. For example, the ammonia ion concentration in the circulating water is 100 pp in the third embodiment.
b, in Example 4, it is 500 ppb. When the concentration of ammonia ions in water exceeds 500 ppb, ammonia is vaporized in the conventional water shower, and the absorption removal rate thereof is significantly reduced (Comparative Example 2). In the table, "air washer" means a water shower.

【0036】[0036]

【表1】 [Table 1]

【0037】[0037]

【表2】 [Table 2]

【0038】[0038]

【表3】 [Table 3]

【0039】[0039]

【表4】 [Table 4]

【0040】[0040]

【表5】 [Table 5]

【0041】[0041]

【表6】 [Table 6]

【0042】[0042]

【表7】 [Table 7]

【0043】[0043]

【表8】 [Table 8]

【0044】[0044]

【表9】 [Table 9]

【0045】[0045]

【表10】 [Table 10]

【0046】[0046]

【表11】 [Table 11]

【0047】[0047]

【表12】 [Table 12]

【0048】[0048]

【発明の効果】本発明に係る空気清浄方法は、以下のよ
うな効果を奏する。 (1)ガス状化学汚染物質の除去効率が高い。 (2)安価な金属製斜行ハニカムの使用により、空気清
浄装置全体がコンパクトになるため、省資源であると共
に、処理コストを大幅に低減できる。 (3)使用する脱イオン水の量が少なくて済むため、脱
イオン水の製造コストやポンプ搬送能力を削減できる。 (4)処理する空気が空気清浄装置を通過する際の圧力
損失が小さいため送風動力を低減できる。 (5)金属製斜行ハニカムを構成する波形状の金属板の
上を流下する水と処理空気とを接触させるため、表面積
の大きなハニカム表面の水だけが蒸発し、一度水に取り
込まれてしまった化学汚染物質は水側に残るので、化学
汚染物質の再飛散は起こり難い。このため、被処理空気
を再汚染する恐れが少ない。 (6)斜行ハニカムが金属製であるため、壁の強度を強
くできるので、該金属製斜行ハニカムの壁を薄くでき
る。 (7)ハニカムの壁を薄くできるので、圧力損失を小さ
くできる。 (8)耐水性や流水による耐摩耗性を含めた耐久性に優
れる。 (9)空気と水の接触を金属製斜行ハニカムを介して行
うため、使用する金属板からのパーティクルが空気に混
入することがないので、クリーンルームへ送る空気の清
浄化に好適である。 (10)空気と水の接触を金属製斜行ハニカムを介して
行うため、使用する金属板からのアウトガスが空気に混
入することがないのでクリーンルームへ送る空気の清浄
化に好適である。 (11)空気と水の接触を金属製斜行ハニカムを介して
行うため、かびや藻類の発生がない。
The air cleaning method according to the present invention has the following effects. (1) Efficient removal of gaseous chemical pollutants. (2) By using an inexpensive metal diagonal honeycomb, the entire air cleaning device becomes compact, which saves resources and greatly reduces the processing cost. (3) Since the amount of deionized water used is small, it is possible to reduce the production cost of deionized water and the pumping capacity. (4) Since the pressure loss when the air to be processed passes through the air cleaning device is small, the blowing power can be reduced. (5) Since the water flowing down on the corrugated metal plate forming the oblique metal honeycomb is brought into contact with the treated air, only the water on the honeycomb surface having a large surface area is evaporated and once taken into the water. Since the chemical pollutants remain on the water side, re-scattering of the chemical pollutants is unlikely to occur. Therefore, there is little risk of recontamination of the air to be treated. (6) Since the oblique honeycomb is made of metal, the strength of the wall can be increased, so that the wall of the oblique metal honeycomb can be made thin. (7) Since the honeycomb wall can be made thin, pressure loss can be reduced. (8) Excellent durability including water resistance and abrasion resistance due to running water. (9) Since air and water are brought into contact with each other through a metal oblique honeycomb, particles from a metal plate to be used are not mixed in the air, which is suitable for cleaning air sent to a clean room. (10) Since air and water are brought into contact with each other through the metal oblique honeycomb, outgas from the metal plate used is not mixed with air, which is suitable for cleaning air to be sent to a clean room. (11) Since air and water are brought into contact with each other through the metal oblique honeycomb, mold and algae are not generated.

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

【図1】本発明の空気清浄方法で使用する金属製斜行ハ
ニカムを説明する図である。
FIG. 1 is a diagram illustrating a metal oblique honeycomb used in the air cleaning method of the present invention.

【符号の説明】[Explanation of symbols]

1 金属製斜行ハニカム 13 加湿手段 23 凝縮手段 101,104 上下両面 102,103 前後両面 1 Metal skewed honeycomb 13 Humidification means 23 Condensing means 101, 104 both upper and lower sides 102, 103 both front and back

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4C080 AA09 BB02 BB05 BB10 CC01 HH03 KK08 LL12 MM01 QQ11 4D020 AA10 BA23 BB03 CB10 CB29 CD10 DA01 DB02 DB12    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4C080 AA09 BB02 BB05 BB10 CC01                       HH03 KK08 LL12 MM01 QQ11                 4D020 AA10 BA23 BB03 CB10 CB29                       CD10 DA01 DB02 DB12

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 前後両面と上下両面とが開口して配置さ
れた金属製斜行ハニカムの前面開口部から化学汚染物質
を含む空気を導入すると共に、 上面開口部から水を供給することで、前記空気を加湿さ
せ、 得られる過剰な水分に化学汚染物質の少なくとも一部を
取り込むことで、空気中から化学汚染物質を除去するこ
とを特徴とする空気清浄方法。
1. Introducing air containing chemical contaminants from a front opening of a metal oblique honeycomb in which front and rear surfaces and upper and lower surfaces are opened, and supplying water from an upper opening, A method for cleaning air, characterized in that the air is humidified and at least a part of the chemical pollutants is taken into the obtained excess water to remove the chemical pollutants from the air.
【請求項2】 前後両面と上下両面とが開口して配置さ
れた金属製斜行ハニカムの前面開口部から化学汚染物質
を含む空気を導入すると共に、 上面開口部から水を供給することで、前記空気を除湿さ
せ、 得られる凝縮水に化学汚染物質の少なくとも一部を取り
込むことで、空気中から化学汚染物質を除去することを
特徴とする空気清浄方法。
2. Introducing air containing a chemical pollutant from a front opening of a metal oblique honeycomb in which front and rear surfaces and upper and lower surfaces are opened, and supplying water from an upper opening, An air cleaning method, wherein the air is dehumidified, and at least a part of the chemical pollutants is taken into the resulting condensed water to remove the chemical pollutants from the air.
【請求項3】 化学汚染物質を含む空気を導入すると共
に、該空気と水とを接触することで、前記空気を加湿さ
せ、 得られる過剰な水分に化学汚染物質の少なくとも一部を
取り込むことで、空気中から化学汚染物質を除去する加
湿工程と、 化学汚染物質を含む空気を導入させ、該空気と水とを接
触することで、前記空気を除湿し、 得られる凝縮水に化学汚染物質の少なくとも一部を取り
込むことで、空気中から化学汚染物質を除去する除湿工
程とを有する空気洗浄方法であって、 加湿工程で使用する加湿手段、及び除湿手段で使用する
凝縮手段として、前後両面と上下両面とが開口して配置
された金属製斜行ハニカムを前記両手段の一方又は両方
に使用することを特徴とする空気清浄方法。
3. By introducing air containing a chemical pollutant and contacting the air with water, the air is humidified, and at least a part of the chemical pollutant is taken into excess water obtained. A humidifying step of removing chemical pollutants from the air, and introducing air containing chemical pollutants, and contacting the air with water to dehumidify the air, and to obtain the condensed water containing chemical pollutants. An air cleaning method having a dehumidifying step of removing chemical pollutants from the air by incorporating at least a part thereof, wherein the front and rear surfaces are used as a humidifying means used in the humidifying step and a condensing means used in the dehumidifying means. A method for air cleaning, characterized in that a skewed metal honeycomb in which both upper and lower surfaces are opened is used for one or both of the both means.
【請求項4】 前後両面と上下両面とが開口して配置さ
れた金属製斜行ハニカムの前面開口部から化学汚染物質
を含む空気を導入すると共に、 上面開口部から水を供給し、 前記金属製斜行ハニカムの前段部で前記空気を加湿さ
せ、 得られる過剰な水分に化学汚染物質の少なくとも一部を
取り込むことで、空気中から化学汚染物質を除去し、 次いで前記空気を除湿させ、得られる凝縮水に化学汚染
物質の少なくとも一部を取り込むことで、空気中から化
学汚染物質を除去することを特徴とする空気清浄方法。
4. The air containing chemical contaminants is introduced from the front opening of a metal diagonal honeycomb having front and rear surfaces and upper and lower surfaces opened, and water is supplied from the upper opening, The air is humidified at the front stage of the oblique manufacturing honeycomb, and at least a part of the chemical pollutants is taken into the excess water obtained, thereby removing the chemical pollutants from the air, and then dehumidifying the air to obtain A method for cleaning air, characterized in that chemical pollutants are removed from the air by incorporating at least part of the chemical pollutants into the condensed water that is generated.
JP2002024290A 2002-01-31 2002-01-31 Air cleaning method Expired - Fee Related JP3716926B2 (en)

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Country Status (1)

Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006192097A (en) * 2005-01-14 2006-07-27 Tohoku Univ Air sterilization and deodorization apparatus
JP2009511856A (en) * 2005-10-18 2009-03-19 ニコライ,ライオネル Air conditioning system with low energy consumption

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006192097A (en) * 2005-01-14 2006-07-27 Tohoku Univ Air sterilization and deodorization apparatus
JP4693422B2 (en) * 2005-01-14 2011-06-01 国立大学法人東北大学 Air sterilization deodorization system
JP2009511856A (en) * 2005-10-18 2009-03-19 ニコライ,ライオネル Air conditioning system with low energy consumption

Also Published As

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