JPH10328519A - Field-free air cleaning method and device therefor - Google Patents
Field-free air cleaning method and device thereforInfo
- Publication number
- JPH10328519A JPH10328519A JP9156100A JP15610097A JPH10328519A JP H10328519 A JPH10328519 A JP H10328519A JP 9156100 A JP9156100 A JP 9156100A JP 15610097 A JP15610097 A JP 15610097A JP H10328519 A JPH10328519 A JP H10328519A
- Authority
- JP
- Japan
- Prior art keywords
- air
- particles
- main body
- chamber
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 24
- 238000004140 cleaning Methods 0.000 title claims abstract description 11
- 239000002245 particle Substances 0.000 claims abstract description 174
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 96
- 239000000428 dust Substances 0.000 claims abstract description 45
- 239000010419 fine particle Substances 0.000 claims description 61
- 238000000926 separation method Methods 0.000 claims description 56
- 239000007921 spray Substances 0.000 claims description 21
- 238000003780 insertion Methods 0.000 claims description 16
- 230000037431 insertion Effects 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 15
- 230000005684 electric field Effects 0.000 claims description 9
- 239000008236 heating water Substances 0.000 claims description 8
- 238000005507 spraying Methods 0.000 claims description 8
- 239000003570 air Substances 0.000 claims 1
- 241000894006 Bacteria Species 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000009834 vaporization Methods 0.000 description 5
- 230000008016 vaporization Effects 0.000 description 5
- 238000001816 cooling Methods 0.000 description 4
- 238000000889 atomisation Methods 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- 241000233866 Fungi Species 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000004065 semiconductor Substances 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 239000002210 silicon-based material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000003075 superhydrophobic effect Effects 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Electrostatic Separation (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、クリーンルー
ム、病院、食品工場、半導体工場、ホテル等の部屋の空
気を無電界にしかつクリーン化する、エアークリーン方
法及びその装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air cleaning method and an air cleaning method for removing air from a room such as a clean room, a hospital, a food factory, a semiconductor factory, a hotel, and the like and eliminating the electric field.
【0002】[0002]
【従来の技術】従来、半導体や薬を扱うクリーンルーム
は四側壁や天井等に微細な網目から成るペパフィルター
を用い、このクリールームにフィルターを通してエアー
を吸引し、2〜3μ以上の微粒子をフィルターで濾過し
ている。2. Description of the Related Art Conventionally, a clean room handling semiconductors and chemicals uses a paper filter formed of a fine mesh on four side walls and a ceiling, etc., and air is sucked through the filter into this clean room to filter fine particles of 2 to 3 μm or more. Filtered.
【0003】[0003]
【発明が解決しようとする課題】しかしながらこのフィ
ルターはよりクリーンなエアーを得ようとすると、粒径
のより小さな微粒子を捕集しなければならず、そのため
網目を小さくしなければならない。このようにすると
2、3ヶ月で捕集した微粒子により網目が詰まり、詰ま
ると温度が上昇し、水分の飽和点が上がる。従って通過
するエアーに水分が多く含まれ、フィルター箇所で結露
が生じる。従ってフィルターは数ヶ月で使用不能にな
り、新しいものに取替えなければならず、極めてコスト
の高いものとなっている。従って粒径の小さな微粒子は
捕集することができず、クリーン化に限度がある。However, in order to obtain cleaner air, this filter has to collect fine particles having a smaller particle size, and therefore has to reduce the mesh size. In this way, the mesh is clogged with the fine particles collected in a few months, and when the mesh is clogged, the temperature rises and the saturation point of the water rises. Therefore, the passing air contains a large amount of moisture, and dew condensation occurs at the filter location. Therefore, the filters become unusable in a few months and must be replaced with new ones, which is extremely costly. Therefore, fine particles having a small particle size cannot be collected, and there is a limit to cleanliness.
【0004】この発明はこれらの点に鑑みてなされたも
のであり、水を微粒子化し、この水の微粒子を単極帯電
させて、エアーに含まれるゴミやチリ等の微粒子と結合
させ、より大きな粒径の水滴とし、これをエアーと分離
させ、エアーを浄化させるとともに無電界にさせる、極
めて効率の良い、エアークリーン方法及びその装置を提
供し上記課題を解決しようとするものである。[0004] The present invention has been made in view of these points, and water is made finer, the fine particles of water are monopolarly charged, and combined with fine particles such as dust and dust contained in air to form a larger particle. It is an object of the present invention to provide an extremely efficient air cleaning method and an apparatus for separating water droplets having a particle size, separating the air from the air, purifying the air and eliminating an electric field, and solving the above problems.
【0005】[0005]
【課題を解決するための手段】そこで請求項1項の発明
は、吸引装置により装置本体のエアー挿入口から入った
エアーに、水の微粒子から成るマイクロゾルを噴霧す
る。これにより霧化による断熱膨張と蒸気化熱による冷
却効果によりエアーは冷却する。またエアーの中は水分
の過飽和状態となる。これらの噴霧された水のマイクロ
ゾルの微粒子は、気化等により浮遊中に粒径が約50μ
以下となり、+−等量に単極帯電し易い状態となる。ま
た一方エアーの中のチリやホコリ等の粒子も静電誘導に
より帯電している。そこでこれらのチリやホコリ等の粒
子と逆の極に単極帯電したマイクロゾルとが相互に吸
引、結合して粒径が大きな水滴となる。また水のマイク
ロゾルの微粒子は単極帯電しない場合もあるが、チリや
ホコリ等の粒子が帯電している場合が多く、これらの帯
電した粒子に引き付けられ、凝集する。Therefore, according to the first aspect of the present invention, a micro sol composed of fine particles of water is sprayed onto air introduced from an air inlet of the apparatus main body by a suction apparatus. Thereby, the air is cooled by adiabatic expansion by atomization and a cooling effect by heat of vaporization. In addition, the air becomes supersaturated with water. The fine particles of these sprayed water microsols have a particle size of about 50μ
As a result, monopolar charging is likely to occur at + -equivalent amounts. On the other hand, particles such as dust and dust in the air are also charged by electrostatic induction. Therefore, these particles such as dust and dust and the microsol charged unipolarly on the opposite pole are mutually attracted and combined to form water droplets having a large particle diameter. Although the water microsol fine particles may not be monopolarly charged, particles such as dust and dust are often charged, and are attracted to these charged particles and aggregate.
【0006】これらの凝集して粒径が大きくなった粒子
乃至は水滴を含むエアーを粒子分離装置に通し、これら
の粒子を捕集し、エアーのなかの微粒子を取り除くこと
によりエアーをクリーン化するとともに無電界とする方
法とした。上記粒子分離装置では、水が付着しやすい水
の膜を設けており、上記凝集して粒径が大きくなった粒
子乃至は水滴はこの水の膜に付着し、エアーと分離され
る。ここで上記マイクロゾルは水の粒子から成るもので
あるが、好ましくは粒径が約50μ以下であり、電気抵
抗が105〜1010Ω程度の純水を使用した方が、単極
帯電しやすい。[0006] Air containing these aggregated particles or water droplets having a large particle diameter is passed through a particle separator to collect these particles and remove the fine particles from the air to clean the air. And a method of eliminating an electric field. In the above-described particle separation device, a water film to which water easily adheres is provided, and the particles or water droplets having a large particle diameter due to aggregation adhere to the water film and are separated from air. Here, the micro sol is composed of water particles, and preferably, pure water having a particle size of about 50 μm or less and an electric resistance of about 10 5 to 10 10 Ω is more monopolar. Cheap.
【0007】請求項2項の発明は、吸引装置により装置
本体のエアー挿入口から入ったエアーと、水を加熱して
成る蒸気とを混ぜる。エアーとこの蒸気とが混ざること
により温度が下がり、蒸気の粒径も大きくなる。そして
この蒸気の微粒子は過飽和状態の中で純度の高い微粒子
のため、また粒径が約50μ以下となるため、+−等量
に単極帯電し易い。また一方エアーの中のチリやホコリ
等の粒子も上述のように帯電している。そこでこれらの
チリやホコリ等の粒子と逆の極に単極帯電した微粒子と
が相互に吸引、結合して粒径が大きくなる。また蒸気の
微粒子は単極帯電しない場合もあるが、チリやホコリ等
の粒子が帯電している場合が多く、これらの帯電した粒
子に引き付けられ、凝集する。これらの凝集して粒径が
大きくなった粒子乃至は水滴を含むエアーを粒子分離装
置に通し、これらの粒子を捕集し、エアーのなかの微粒
子を取り除くことによりエアーをクリーン化するととも
に無電界とする方法とした。なおこの粒子分離装置は上
記請求項1項の発明のものと同様のものである。According to a second aspect of the present invention, the air introduced from the air inlet of the apparatus main body by the suction device is mixed with steam formed by heating water. Mixing the air and the steam lowers the temperature and increases the particle size of the steam. Since the fine particles of the vapor are fine particles having a high purity in a supersaturated state and have a particle size of about 50 μm or less, they are easily unipolarly charged to + -equivalent amounts. On the other hand, particles such as dust and dust in the air are also charged as described above. Thus, the particles such as dust and dust are attracted and combined with each other by the unipolarly charged fine particles on the opposite pole to increase the particle size. Further, the vapor fine particles may not be monopolarly charged, but in many cases, particles such as dust and dust are charged, and are attracted to these charged particles and aggregate. The air containing these aggregated particles or water droplets having a large particle diameter is passed through a particle separation device to collect these particles and remove the fine particles from the air to clean the air and to reduce the electric field. Was adopted. This particle separation device is the same as that of the first aspect of the present invention.
【0008】請求項3項の発明は、吸引装置により装置
本体のエアー挿入口から入ったエアーに、水の微粒子か
ら成るマイクロゾルを噴霧させる。これにより霧化によ
る断熱膨張と蒸気化熱による冷却効果によりエアーは冷
却する。またエアーの中は水分の過飽和状態となる。ま
たこれらの噴霧された水のマイクロゾルの微粒子は、気
化等により浮遊中に粒径が約50μ以下となり、+−等
量に単極帯電し易い状態となる。また一方エアーの中の
チリやホコリ等の粒子も上述のように帯電している。そ
こでエアー中のチリやホコリ等の帯電した粒子と逆の極
に単極帯電したマイクロゾルとが相互に吸引、結合して
粒径が大きな水滴となる。また水のマイクロゾルの微粒
子は単極帯電しない場合もあるが、チリやホコリ等の粒
子が帯電している場合が多く、これらの帯電した粒子に
引き付けられ、凝集する。これらの凝集して粒径が大き
くなった粒子乃至は水滴を含むエアーを粒子分離装置に
通す。この粒子分離装置は当該エアーの挿通方向と平行
に複数枚の板体を間隔をあけて相対向して並べ、これら
の各板体の間隔を二層流が生じる巾とし、この二層流式
粒子分離装置により微粒子を捕集し、エアーのなかの微
粒子を取り除くことによりエアーをクリーン化するとと
もに無電界とする方法とした。According to a third aspect of the present invention, a micro sol composed of fine particles of water is sprayed on air entered from an air inlet of the apparatus main body by a suction device. Thereby, the air is cooled by adiabatic expansion by atomization and a cooling effect by heat of vaporization. In addition, the air becomes supersaturated with water. The fine particles of these sprayed water microsols have a particle size of about 50 μm or less during suspension due to vaporization or the like, and are likely to be unipolarly charged to + -equivalent amounts. On the other hand, particles such as dust and dust in the air are also charged as described above. Then, the charged particles such as dust and dust in the air and the monopolarly charged microsol on the opposite pole are mutually attracted and combined to form water droplets having a large particle diameter. Although the water microsol fine particles may not be monopolarly charged, particles such as dust and dust are often charged, and are attracted to these charged particles and aggregate. The air containing these aggregated particles or water droplets having an increased particle size is passed through a particle separator. In this particle separation device, a plurality of plates are arranged in parallel with each other at an interval in parallel with the air insertion direction, and the interval between these plates is set to a width at which a two-layer flow is generated. Fine particles were collected by a particle separator, and the air was cleaned by removing the fine particles in the air, and the method was applied to eliminate the electric field.
【0009】請求項4項の発明は、吸引装置により装置
本体のエアー挿入口から入ったエアーと、水を加熱して
成る蒸気とを混ぜる。この蒸気の粒子は過飽和状態の中
で純度の高い微粒子のため、また粒径が約50μ以下と
なるため、+−等量に単極帯電し易く、エアー中のチリ
やホコリ等の帯電した粒子と上記単極帯電した粒子とが
相互に吸引、結合して粒径が大きくなる。また蒸気の微
粒子は単極帯電しない場合もあるが、チリやホコリ等の
粒子が帯電している場合が多く、これらの帯電した粒子
に引き付けられ、凝集する。これらの凝集して粒径が大
きくなった粒子を含むエアーを粒子分離装置に通す。こ
の粒子分離装置は当該エアーの挿通方向と平行に複数枚
の板体を間隔をあけて相対向して並べ、これらの各板体
の間隔を二層流が生じる巾とし、この二層流式粒子分離
装置により微粒子を捕集し、エアーのなかの微粒子を取
り除くことによりエアーをクリーン化するとともに無電
界とする方法とした。According to a fourth aspect of the present invention, the air introduced from the air inlet of the apparatus main body by the suction device is mixed with steam formed by heating water. Since the vapor particles are fine particles of high purity in a supersaturated state, and have a particle size of about 50 μm or less, they are easily monopolarly charged to + -equivalent amounts, and are charged particles such as dust and dust in the air. And the monopolar charged particles are mutually attracted and combined to increase the particle size. Further, the vapor fine particles may not be monopolarly charged, but in many cases, particles such as dust and dust are charged, and are attracted to these charged particles and aggregate. The air containing these aggregated particles having an increased particle size is passed through a particle separator. In this particle separation device, a plurality of plate members are arranged in parallel with each other at an interval in parallel with the air insertion direction, and the interval between these plate members is set to a width at which a two-layer flow is generated. Fine particles were collected by a particle separator, and the air was cleaned by removing the fine particles in the air, and the method was applied to eliminate the electric field.
【0010】請求項5項の発明は、中空の装置本体のエ
アー挿入口につづく部屋に水を噴霧するノズルを設け、
この噴霧室につづき、エアーのなかの水滴又は粒子をエ
アーと分離する粒子分離装置室を設け、この粒子分離装
置室は水が付着しやすい水の膜を設けており、これらの
噴霧室及び粒子分離装置室を一対又は複数対設け、この
装置本体内又は装置本体の排出口後方に吸引装置を設け
た、無電界エアークリーン装置とした。According to a fifth aspect of the present invention, there is provided a nozzle for spraying water into a room following an air insertion port of a hollow apparatus main body,
Following the spray chamber, a particle separator chamber for separating water droplets or particles in the air from the air is provided, and the particle separator chamber is provided with a water film to which water easily adheres. One or more pairs of separation device chambers were provided, and a suction device was provided in the device main body or behind the outlet of the device main body.
【0011】請求項6項の発明は、中空の装置本体のエ
アー挿入口につづく部屋に、水を加熱して成る蒸気とを
混合する混合室を設け、この混合室につづき、エアーの
なかの水滴又は粒子をエアーと分離する粒子分離装置室
を設け、この粒子分離装置室は水が付着しやすい水の膜
を設けており、これらの混合室及び粒子分離装置室を一
対又は複数対設け、この装置本体内又は装置本体の排出
口後方に吸引装置を設けた、無電界エアークリーン装置
とした。According to a sixth aspect of the present invention, a mixing chamber for mixing water formed by heating water is provided in a room following an air insertion port of a hollow apparatus main body. Providing a particle separation device chamber for separating water droplets or particles from air, the particle separation device room is provided with a water film to which water easily adheres, and one or more pairs of these mixing rooms and particle separation device rooms are provided, An electric field-free air-cleaning device was provided with a suction device in the apparatus main body or behind the discharge port of the apparatus main body.
【0012】請求項7項の発明は、中空の装置本体のエ
アー挿入口につづく部屋に水を噴霧するノズルを設け、
この噴霧室につづき、エアーのなかの水滴又は粒子をエ
アーと分離する粒子分離装置室を設け、この粒子分離装
置室にはエアーの流通方向と平行に複数枚の板体を相互
に間隔をあけて相対向して並べ設け、これらの各板体の
間隔を二層流が生じる巾とし、これらの噴霧室及び粒子
分離装置室を一対又は複数対設け、この装置本体内又は
装置本体の排出口後方に吸引装置を設けた、無電界エア
ークリーン装置とした。The invention according to claim 7 is provided with a nozzle for spraying water into a room following the air insertion port of the hollow apparatus main body,
Following the spray chamber, a particle separation device chamber for separating water droplets or particles in the air from the air is provided, and a plurality of plates are spaced apart from each other in the particle separation device room in parallel with the direction of air flow. And a space between these plates is set to a width at which a two-layer flow is generated, and a pair or a plurality of pairs of the spray chambers and the particle separation device chambers are provided. An electric field-free air clean device provided with a suction device behind.
【0013】請求項8項の発明は、中空の装置本体のエ
アー挿入口につづく部屋に、水を加熱して成る蒸気とを
混合する混合室を設け、この混合室につづき、エアーの
なかの水滴又は粒子をエアーと分離する粒子分離装置室
を設け、この粒子分離装置室にはエアーの流通方向と平
行に複数枚の板体を相互に間隔をあけて相対向して並べ
設け、これらの各板体の間隔を二層流が生じる巾とし、
これらの混合室及び粒子分離装置室を一対又は複数対設
け、この装置本体内又は装置本体の排出口後方に吸引装
置を設けた、無電界エアークリーン装置とした。According to the invention of claim 8, a mixing chamber for mixing steam formed by heating water is provided in a room following the air insertion port of the hollow apparatus main body. A particle separation device chamber for separating water droplets or particles from air is provided, and a plurality of plate bodies are arranged in this particle separation device room in parallel with each other in parallel with the flow direction of air at intervals. The interval between each plate is the width at which a two-layer flow occurs,
One or more pairs of the mixing chamber and the particle separating apparatus chamber were provided, and a suction device was provided in the apparatus main body or behind the discharge port of the apparatus main body, to form an electric field-free air clean apparatus.
【0014】[0014]
【発明の実施の形態例】以下この発明の実施の形態例を
図に基づいて説明する。まずこの発明の装置につき図1
に基づいて説明すると、装置本体1の上部にはエアー流
通路2を蛇行形状に設け、また下部には水のタンク3を
設けている。このエアー流通路2の一端にはエアー挿入
口4を設け、このエアー挿入口4につづき、水を噴霧す
る第1ノズル5を有する第1噴霧室6が、またこの第1
噴霧室6につづき、第1粒子分離装置室7が設けられて
いる。Embodiments of the present invention will be described below with reference to the drawings. First, FIG.
The air flow passage 2 is provided in a meandering shape at the upper part of the apparatus main body 1, and a water tank 3 is provided at the lower part. An air insertion port 4 is provided at one end of the air flow passage 2, and a first spray chamber 6 having a first nozzle 5 for spraying water is connected to the air insertion port 4.
Following the spray chamber 6, a first particle separation device chamber 7 is provided.
【0015】さらに純水を噴霧する第2ノズル8を有す
る第2噴霧室9が設けられ、これにつづいて第2粒子分
離装置室10が設けられている。またさらにこの第2粒
子分離装置室10につづき第3粒子分離装置室11、さ
らにエアー排気口12が夫々設けられている。また上記
タンク3は第1タンク3aと第2タンク3bとに分かれ
ている。第1タンク3aには液注入口13から電気抵抗
が105〜1010Ω程度の純水が注入されている。そし
てこの第1タンク3aからフィルター14aを介してポ
ンプ14により純水を引上げ、これを上記第2ノズル8
から第2噴霧室9に粒径50μ以下であって粒径を均一
にそろえたマイクロゾルとして噴霧するようになってい
る。Further, a second spray chamber 9 having a second nozzle 8 for spraying pure water is provided, followed by a second particle separation device chamber 10. Further, a third particle separation chamber 11, and an air exhaust port 12 are provided after the second particle separation chamber 10. The tank 3 is divided into a first tank 3a and a second tank 3b. Pure water having an electric resistance of about 10 5 to 10 10 Ω is injected into the first tank 3a from the liquid inlet 13. Then, pure water is pulled up from the first tank 3a by the pump 14 through the filter 14a, and the pure water is pulled up by the second nozzle 8
Thus, the micro sol having a particle diameter of 50 μm or less and having a uniform particle diameter is sprayed into the second spray chamber 9.
【0016】また上記第2タンク3bには上記第1噴霧
室6、第1粒子分離装置室7、第2噴霧室9、第2粒子
分離装置室10及び第3粒子分離装置室11から夫々ド
レイン排出パイプ15a、15b、15cが導入され、
夫々の部屋のドレインを集める構成と成っている。そし
てこの第2タンク3bから揚水パイプ16により図外の
ポンプを介して水を引上げ第1ノズル5から第1噴霧室
6にマイクロゾルを噴霧するように成っている。また装
置本体1のエアー排気口12につづき、ブロアー17を
設け、このブロアー17により、上記エアー流通路2の
エアーの流れを作っている。このブロアー17につづ
き、エアーを均一化する拡散ボックス18を備えてい
る。The second tank 3b is provided with a drain from the first spray chamber 6, the first particle separator chamber 7, the second spray chamber 9, the second particle separator chamber 10, and the third particle separator chamber 11, respectively. Discharge pipes 15a, 15b, 15c are introduced,
It consists of collecting drains in each room. Then, water is pulled up from the second tank 3b by a pumping pipe 16 via a pump (not shown), and the micro sol is sprayed from the first nozzle 5 to the first spray chamber 6. A blower 17 is provided following the air exhaust port 12 of the apparatus main body 1, and the blower 17 creates an air flow in the air flow passage 2. Following the blower 17, a diffusion box 18 for uniformizing air is provided.
【0017】上記各粒子分離装置室7、10、11内の
粒子分離装置は、図2に示す如く、エアーの流れる方向
に略平行な多数の薄板19を間隔をあけて相対向して並
べ設け、これらの各隣接する薄板19の間隔を極めて小
さくし、二層流の生じる間隔とする。これらの薄板19
の間にエアーを流すと、図3に示す如く、エアーの流れ
の中に各薄板19の表面に沿って固定層20が生じ、こ
れらの間に流動層21ができる。この固定層20は粘度
が高く、流動層21内の微粒子はこれらの固定層20に
当たって減速される。これにより各粒子分離装置をエア
ーが通ると、エアー中の固形微粒子の一部は上記固定層
20に接触して減速し、下方に落下していく。この粒子
分離装置の薄板19の素材は、木の板、金属板、有機材
料から成る板、カーボン繊維等の無機材料から成る板、
ウッドセラミックから成る板等がある。As shown in FIG. 2, the particle separators in each of the particle separator chambers 7, 10, 11 are provided with a number of thin plates 19 which are substantially parallel to the direction in which air flows and are arranged opposite to each other at intervals. The distance between these adjacent thin plates 19 is made extremely small to make a two-layer flow. These thin plates 19
As shown in FIG. 3, when air flows between the thin plates 19, a fixed layer 20 is formed along the surface of each thin plate 19 in the flow of air, and a fluidized layer 21 is formed between these. The fixed layer 20 has a high viscosity, and the fine particles in the fluidized bed 21 hit these fixed layers 20 and are decelerated. As a result, when the air passes through each particle separating device, a part of the solid fine particles in the air comes into contact with the fixed layer 20, decelerates, and falls downward. The material of the thin plate 19 of this particle separation device is a wooden plate, a metal plate, a plate made of an organic material, a plate made of an inorganic material such as carbon fiber,
There is a plate made of wood ceramic, and the like.
【0018】これにより複数の粒子分離装置室7、1
0、11を通過すると、エアー中の微粒子がエアーから
分離される構成となっている。As a result, a plurality of particle separation chambers 7, 1
When passing through 0 and 11, fine particles in the air are separated from the air.
【0019】つぎにこの発明の方法を説明する。上記ブ
ロアー17の吸引力により装置本体1のエアー挿入口4
からエアーが吸引され、第1噴霧室6に入る。そこでは
第2タンク3bから汲み上げた水を第1ノズル5により
粒径が約50μ以下であってかつ粒径の均一なマイクロ
ゾルとして噴霧される。この霧化による断熱膨張と蒸気
化熱による冷却効果により第1噴霧室6内のエアーは冷
却される。またこれにより第1噴霧室6内は水分の過飽
和状態となり、この中での水のマイクロゾルの粒子は+
−等量に単極帯電する。そこでエアーの中の単極帯電し
たチリやホコリ等の粒子と逆の極に単極帯電したマイク
ロゾルとが相互に吸引、結合して粒径が大きな水滴とな
る。また水を粒径50μ以下のマイクロゾルにした場合
又は純水に界面活性剤を入れたものを同様にマイクロゾ
ルとした場合等これらの粒子はすべて帯電する訳ではな
い。しかしながらホコリ等の濾過したい微粒子はプラ
ス、マイナスどちらかの極に帯電しているので、上記水
のマイクロゾルの粒子はこれらに吸引される。Next, the method of the present invention will be described. The suction force of the blower 17 causes the air inlet 4
And the air enters the first spray chamber 6. There, water pumped from the second tank 3b is sprayed by the first nozzle 5 as a microsol having a particle size of about 50 μm or less and having a uniform particle size. The air in the first spray chamber 6 is cooled by the adiabatic expansion by the atomization and the cooling effect by the heat of vaporization. In addition, the inside of the first spraying chamber 6 is in a supersaturated state of water, and the particles of the microsol in the water are +
-Unipolar charging to an equal amount. Then, the monopolar charged particles such as dust and dust in the air and the monopolar charged microsol on the opposite pole are mutually attracted and combined to form a water droplet having a large particle diameter. Not all of these particles are charged, for example, when water is made into a microsol having a particle size of 50 μm or less or when pure water containing a surfactant is similarly made into a microsol. However, the fine particles to be filtered, such as dust, are charged to either the positive or negative pole, so that the water microsol particles are sucked by these.
【0020】これらの凝集して粒径が大きくなった水滴
を含むエアーを第1粒子分離装置室7に通し、ここで上
述の如く微粒子を捕集し、エアーのなかの微粒子を取り
除く。そしてエアーはさらに第2噴霧室9に入ると、第
1タンク3aから汲み上げた純水が第2ノズル8から再
び粒径が約50μ以下であってかつ粒径の均一なマイク
ロゾルとして噴霧される。これにより上述と同様第2噴
霧室9内エアーはさらに冷却され水分の過飽和状態とな
る。またこの中での水のマイクロゾルの粒子は+−等量
に単極帯電する。そこで上記第1粒子分離装置室7で除
去出来なかったエアーの中のチリやホコリ等の粒子も単
極帯電しており、これらのチリやホコリ等の粒子と逆の
極に単極帯電したマイクロゾルとが相互に吸引、結合し
て粒径が大きな水滴となる。そしてこの水滴を含んだエ
アーは第2粒子分離装置室10及び第3粒子分離装置室
11に入っていき、水滴は落下して分離され、微粒子を
含まないクリーン化したエアーのみがエアー排気口12
から出ていき、ブロアー17及び拡散ボックス18を経
て排出される。The air containing the water droplets having a large particle diameter due to the aggregation is passed through the first particle separation device chamber 7, where the fine particles are collected as described above, and the fine particles in the air are removed. Then, when the air further enters the second spray chamber 9, the pure water pumped from the first tank 3a is sprayed again from the second nozzle 8 as a microsol having a particle diameter of about 50 μm or less and a uniform particle diameter. . As a result, the air in the second spray chamber 9 is further cooled as described above, and becomes in a supersaturated state of water. Further, the particles of the microsol in the water are monopolarly charged to + -equivalent amounts. Therefore, particles such as dust and dust in the air that could not be removed in the first particle separation device chamber 7 are also monopolarly charged. The sol and the sol mutually suck and combine to form water droplets having a large particle size. Then, the air containing the water droplets enters the second particle separation device chamber 10 and the third particle separation device room 11, and the water droplets are dropped and separated, and only the clean air containing no fine particles is supplied to the air exhaust port 12.
And is discharged through a blower 17 and a diffusion box 18.
【0021】なお上記実施の形態例では、水又は純水を
約50μ以下の粒径のマイクロゾルとして、エアー流通
経路2において二箇所で噴霧し、夫々において粒子分離
装置を通して微粒子を分離しているが、これに限らず適
宜回数の噴霧及び粒子分離装置による微粒子の除去を繰
り返しても良い。また排出されたエアーが湿度が高すぎ
る場合、冷凍機を用いてエアーの温度を下げて脱水し、
これをクリーンルーム等に放っても良い。また多数の粒
子分離装置に通し、摩擦することによって温度を上げ、
湿度を下げることもできる。また暖房にする場合、マイ
クロゾルにする水の温度をヒーター等で上げ、これをマ
イクロゾルとして噴霧し、エアーの温度を上げて排出す
ることもできる。In the above embodiment, water or pure water is sprayed as microsol having a particle diameter of about 50 μm or less at two places in the air flow path 2 and fine particles are separated through a particle separation device in each case. However, the present invention is not limited thereto, and the spraying and the removal of the fine particles by the particle separating device may be repeated as appropriate. Also, if the discharged air is too high in humidity, use a refrigerator to lower the temperature of the air and dehydrate,
This may be released to a clean room or the like. In addition, we pass through many particle separation devices and raise temperature by friction,
It can also reduce humidity. In the case of heating, it is also possible to raise the temperature of the water to be microsol by a heater or the like, spray this as microsol, and raise the temperature of the air to discharge.
【0022】また上記実施の形態例では、エアーのなか
の水滴又は微粒子を除去する方法として二層流式粒子分
離装置を用いたが、これに限らずセラミックス、金属、
石等の球体又は塊を重ねた中をエアーを通す粒子分離装
置等、適宜の粒子分離装置を用いても良い。またこれら
の各粒子分離装置において、この方法を繰返し連続して
行えば、各粒子分離装置内は湿度の高いエアーが通過す
るため、水の膜が形成される。また強いて各粒子分離装
置に常時又は断続的に水をかけておき、水の膜を形成し
ておいてもよい。この様にすればエアー中の水滴が付着
しやすく、微粒子の捕集がより容易である。この場合、
表面張力をコントロールして水が膜に成りやすいように
する。これにはマイクロゾルにする水に界面活性剤を入
れる場合と粒子分離板そのものの表面に界面活性剤を塗
布して、その表面張力をコントロールする場合がある。
またこの装置の最終段階では湿度が過飽和の状態でエア
ーがでてくるので、末端の粒子分離装置では超撥水性の
表面加工した分離板等を用いることによって効率良く除
湿できる。この超撥水性の表面はフッ素、シリコン系の
化合物又はその共重合体の膜を形成することにより、分
離板等の表面に水の膜が出来にくくなるようにし、分離
板等に当たった水分を水滴にして下方に落として、エア
ーの除湿をして外部に排気するようにしてもよい。In the above embodiment, a two-layer flow type particle separator is used as a method for removing water droplets or fine particles in air. However, the present invention is not limited to this.
An appropriate particle separation device such as a particle separation device that passes air through a pile of spheres or blocks such as stones may be used. In addition, if this method is repeatedly and continuously performed in each of these particle separation devices, a humid air passes through each particle separation device, so that a water film is formed. Alternatively, water may be constantly or intermittently applied to each particle separation device to form a water film. This makes it easier for water droplets in the air to adhere, making it easier to collect fine particles. in this case,
The surface tension is controlled so that water easily forms a film. For this purpose, there are a case where a surfactant is added to water to be made into a microsol and a case where a surfactant is applied to the surface of the particle separation plate itself to control the surface tension.
In the final stage of this apparatus, air comes out in a state of supersaturated humidity. Therefore, in the terminal particle separation apparatus, dehumidification can be performed efficiently by using a separation plate or the like having a super-hydrophobic surface treatment. By forming a film of fluorine, a silicon-based compound or a copolymer thereof on the surface of the super-water-repellent material, it is difficult to form a water film on the surface of the separation plate, etc. You may make it drop a water drop, and it may make it dehumidify air and exhaust it outside.
【0023】また上記実施の形態例では、水をマイクロ
ゾルにして噴霧しているが、これには水を高圧エアーを
使ってミスト化する方法、ポンプの水圧を利用してミス
ト化する方法、流入空気圧及び流速を利用してミスト化
する方法等、適宜の方法が使用できる。またこれらに替
えて、水を加熱して蒸気を作りこれとエアーとを混ぜて
送る方法もある。いずれの場合も、エアー中のチリやホ
コリ等の粒子と遭遇する際は、水の微粒子の粒径が約5
0μ以下と成っていると単極帯電しやすく、この状態に
することが好ましい。In the above embodiment, water is sprayed in the form of a micro sol. This includes a method of converting water into mist using high-pressure air, a method of forming mist using water pressure of a pump, An appropriate method such as a method of forming mist using the inflow air pressure and the flow velocity can be used. Alternatively, there is a method in which water is heated to form steam, which is then mixed with air and sent. In any case, when encountering particles such as dust and dust in the air, the water
When the thickness is 0 μm or less, monopolar charging is liable to occur, and it is preferable to be in this state.
【0024】[0024]
【発明の効果】請求項1項及び5項の発明は、水を噴霧
して微粒子化し、これにより水の微粒子が単極帯電する
ため、エアーに含まれ、単極帯電したゴミやチリ等の微
粒子がこれらと結合し、より大きな粒径の水滴になる。
この大きな粒径の水滴を粒子分離装置に通し、エアーと
分離させるもので、従来の如く、微粒子を取り除くた
め、フィルターの網目を小さくする必要がない。しかも
どんな粒径の微粒子でも、大径の微粒子にして捕集する
ため、捕集乃至は除去が極めて容易、かつ確実である。
従って粒子分離装置の目づまりが生じない。また細菌
類、真菌類、バクテリア、ビールス菌等はチリやホコリ
等の微粒子に付着しているため、これらのものもこの方
法により分離、除去できる。さらに水の微粒子を単極帯
電させて、上述の様に逆の極に帯電したゴミやチリ等の
微粒子と結合させるため、無電荷の状態となる。それ故
エアーを浄化させるとともに無電界にさせる、極めて効
率の良い方法である。さらに水を噴霧すると、霧化した
状態で断熱膨張による温度の降下と蒸気化熱による冷却
効果によりエアーは冷却される。従って排出されるエア
ーはクリーン化されると同時に冷却されている。According to the first and fifth aspects of the present invention, water is atomized into fine particles, and the fine particles of water are monopolarly charged. Fine particles combine with these to form larger sized water droplets.
The water droplets having the large particle diameter are passed through a particle separation device to be separated from air, so that it is not necessary to reduce the size of the filter network in order to remove the fine particles as in the related art. Moreover, since fine particles of any particle size are collected as large-sized fine particles, collection or removal is extremely easy and reliable.
Therefore, clogging of the particle separation device does not occur. In addition, bacteria, fungi, bacteria, bacterium and the like adhere to fine particles such as dust and dirt, and these can be separated and removed by this method. Further, the water fine particles are monopolarly charged and combined with fine particles such as dust and dust charged to the opposite polarity as described above, so that they are in a non-charged state. Therefore, it is an extremely efficient method of purifying air and eliminating an electric field. When water is further sprayed, the air is cooled by the temperature drop due to adiabatic expansion and the cooling effect by the heat of vaporization in the atomized state. Therefore, the discharged air is cleaned and cooled at the same time.
【0025】請求項2項及び6項の発明は、水を加熱し
て蒸気化して微粒子とし、これにより水の微粒子がエア
ー中で単極帯電するため、エアーに含まれるゴミやチリ
等の微粒子がこれと結合し、より大きな粒径の水滴にし
て、この大きな粒径の水滴を粒子分離装置に通し、エア
ーと分離させるもので、従来の如く、微粒子を取り除く
ため、フィルターの網目を小さくする必要がない。しか
もどんな粒径の微粒子でも、大径の微粒子にして捕集す
るため、捕集乃至は除去が極めて容易、かつ確実であ
る。従って粒子分離装置の目づまりが生じない。また微
粒子に付着している細菌類、真菌類、バクテリア、ビー
ルス菌等はエアーに混ぜられた加熱蒸気により死滅する
が、これで死滅しなかった細菌類等は、微粒子の分離、
除去により除去できる。さらに水の微粒子を単極帯電さ
せて、上述の様に逆の極に帯電したゴミやチリ等の微粒
子と結合させるため、無電荷の状態となる。それ故エア
ーを浄化させるとともに無電界にさせる、極めて効率の
良い方法である。According to the second and sixth aspects of the present invention, since water is vaporized by heating to form fine particles, the fine particles of water are monopolarly charged in the air. Combined with this, water droplets of a larger particle size are formed, and the water droplets of the larger particle size are passed through a particle separation device and separated from air, and as in the conventional case, the mesh of the filter is reduced to remove fine particles. No need. Moreover, since fine particles of any particle size are collected as large-sized fine particles, collection or removal is extremely easy and reliable. Therefore, clogging of the particle separation device does not occur. Bacteria, fungi, bacteria, virus, etc. attached to the microparticles are killed by the heated steam mixed with air, but bacteria not killed by this are separated,
It can be removed by removal. Further, the water fine particles are monopolarly charged and combined with fine particles such as dust and dust charged to the opposite polarity as described above, so that they are in a non-charged state. Therefore, it is an extremely efficient method of purifying air and eliminating an electric field.
【0026】請求項3項及び7項の発明は、上記請求項
1項の発明の効果に加え、薄板をエアーの流れと平行に
並べた二層流式粒子分離装置を通すため、従来の網目に
よるフィルターと異なり、目詰まりが生じにくくまたこ
の網目を通すために特別に圧力をかける必要がない。According to the third and seventh aspects of the present invention, in addition to the effect of the first aspect of the present invention, a thin plate is passed through a two-layer flow type particle separation device arranged in parallel with the flow of air. Unlike the filter according to (1), clogging is less likely to occur, and no special pressure needs to be applied to pass through the mesh.
【0027】請求項4項及び8項の発明は、上記請求項
2項の発明の効果に加え、薄板をエアーの流れと平行に
並べた二層流式粒子分離装置を通すため、従来の網目に
よるフィルターと異なり、目詰まりが生じにくくまたこ
の網目を通すために特別に圧力をかける必要がない。According to the fourth and eighth aspects of the present invention, in addition to the effect of the second aspect of the present invention, a thin plate is passed through a two-layer flow type particle separation device arranged in parallel with the flow of air. Unlike the filter according to (1), clogging is less likely to occur, and no special pressure needs to be applied to pass through the mesh.
【図1】この発明の実施の形態例の概略構成図である。FIG. 1 is a schematic configuration diagram of an embodiment of the present invention.
【図2】この発明の二層流式粒子分離装置の斜視図であ
る。FIG. 2 is a perspective view of a two-layer flow type particle separation device of the present invention.
【図3】この発明の二層流式粒子分離装置の機能原理図
である。FIG. 3 is a functional principle diagram of the two-layer flow type particle separation device of the present invention.
1 装置本体 2 エアー流通
路 3 タンク 4 エアー挿入
口 5 第1ノズル 6 第1噴霧室 7 第1粒子分離装置室 8 第2ノズル 9 第2噴霧室 10 第2粒子分
離装置室 11 第3粒子分離装置室 12 エアー排
気口 17 ブロアー 19 薄板 20 固定層 21 流動層DESCRIPTION OF SYMBOLS 1 Apparatus main body 2 Air flow path 3 Tank 4 Air insertion port 5 1st nozzle 6 1st spray chamber 7 1st particle separation device room 8 2nd nozzle 9 2nd spray room 10 2nd particle separation device room 11 3rd particle separation Equipment room 12 Air exhaust port 17 Blower 19 Thin plate 20 Fixed layer 21 Fluidized bed
Claims (8)
ーに、水の微粒子から成るマイクロゾルを噴霧し、この
エアーの中でマイクロゾルの微粒子を単極帯電させ、エ
アー中のチリやホコリ等の粒子と上記単極帯電したマイ
クロゾルとを相互に吸引、結合させ、これらの凝集した
粒子を含むエアーを粒子分離装置に通し、粒径の大きく
なった粒子を捕集し、エアーのなかの微粒子を取り除く
ことによりエアーをクリーン化することを特徴とする、
無電界エアークリーン方法。1. A microsol composed of fine particles of water is sprayed on air entering from an air insertion port of an apparatus main body, and the microsol fine particles are monopolarly charged in the air, and dust or the like in the air is charged. Particles and the above monopolarly charged microsol are mutually sucked and combined, and the air containing these aggregated particles is passed through a particle separator to collect the particles having an increased particle diameter, and the air is collected in the air. The feature is to clean the air by removing fine particles,
Electric field-free air clean method.
ーと、水を加熱して成る蒸気とを混ぜ、この蒸気の微粒
子を単極帯電させ、エアー中のチリやホコリ等の粒子と
上記単極帯電した微粒子とを相互に吸引、結合させ、こ
れらの凝集した粒子を含むエアーを粒子分離装置に通
し、粒径の大きくなった粒子を捕集し、エアーのなかの
微粒子を取り除くことによりエアーをクリーン化するこ
とを特徴とする、無電界エアークリーン方法。2. An air inlet through an air inlet of the apparatus main body and steam formed by heating water are mixed, and fine particles of the steam are monopolarly charged, and particles such as dust and dust in the air are mixed with the air. The charged particles are attracted and combined with each other, and the air containing these agglomerated particles is passed through a particle separator to collect the particles having a larger particle size and remove the fine particles from the air. An electric field-free air clean method, characterized by cleaning.
ーに、水の微粒子から成るマイクロゾルを噴霧し、この
エアーの中でマイクロゾルの微粒子を単極帯電させ、エ
アー中のチリやホコリ等の粒子と上記単極帯電したマイ
クロゾルとを相互に吸引、結合させ、これらの凝集した
粒子を含むエアーを、当該エアーの挿通方向と平行に複
数枚の板体を間隔をあけて相対向して並べ、これらの各
板体の間隔を二層流が生じる巾とした粒子分離装置に通
し、この二層流式粒子分離装置により粒径の大きくなっ
た粒子を捕集し、エアーのなかの微粒子を取り除くこと
によりエアーをクリーン化することを特徴とする、無電
界エアークリーン方法。3. A microsol composed of fine particles of water is sprayed on air entering through an air inlet of the apparatus main body, and the fine particles of the microsol are monopolarly charged in the air, and dust, dust and the like in the air are sprayed. Particles and the above-mentioned monopolarly charged microsol are mutually attracted and combined, and air containing these aggregated particles is opposed to each other at intervals of a plurality of plates in parallel with the direction of insertion of the air. The two plates are separated and passed through a particle separator with the width of the two-layer flow generated, and the particles having a larger particle size are collected by the two-layer flow particle separator, and are collected in air. An electric field-free air cleaning method characterized in that air is cleaned by removing fine particles.
ーと、水を加熱して成る蒸気とを混ぜ、この蒸気の微粒
子を単極帯電させ、エアー中のチリやホコリ等の粒子と
上記単極帯電した微粒子とを相互に吸引、結合させ、こ
れらの凝集した粒子を含むエアーを、当該エアーの挿通
方向と平行に複数枚の板体を間隔をあけて相対向して並
べ、これらの各板体の間隔を二層流が生じる巾とした粒
子分離装置に通し、この二層流式粒子分離装置により粒
径の大きくなった粒子を捕集し、エアーのなかの微粒子
を取り除くことによりエアーをクリーン化することを特
徴とする、無電界エアークリーン方法。4. An air inlet through an air inlet of the apparatus main body and steam formed by heating water are mixed, and fine particles of the steam are monopolarly charged, and particles such as dust and dust in the air are mixed with the air. The finely charged particles are mutually attracted and combined, and the air containing these agglomerated particles is arranged face to face with a plurality of plates spaced in parallel with the direction of insertion of the air. The gap between the plates is passed through a particle separator that has a width that produces a two-layer flow, and the particles having a larger particle size are collected by the two-layer flow particle separator, and the fine particles in the air are removed to remove air. An electric field-free air clean method, characterized by cleaning.
部屋に水を噴霧するノズルを設け、この噴霧室につづ
き、エアーのなかの水滴又は粒子をエアーと分離する粒
子分離装置室を設け、これらの噴霧室及び粒子分離装置
室を一対又は複数対設け、この装置本体内又は装置本体
の排出口後方に吸引装置を設けたことを特徴とする、無
電界エアークリーン装置。5. A nozzle for spraying water is provided in a chamber following the air insertion port of the hollow apparatus main body, and a particle separation apparatus chamber for separating water droplets or particles in the air from the air is provided following the spray chamber. An electric field-free air-cleaning apparatus characterized in that a pair or a plurality of pairs of the spray chamber and the particle separation apparatus chamber are provided, and a suction device is provided in the apparatus main body or behind the outlet of the apparatus main body.
部屋に、水を加熱して成る蒸気とを混合する混合室を設
け、この混合室につづき、エアーのなかの水滴又は粒子
をエアーと分離する粒子分離装置室を設け、これらの混
合室及び粒子分離装置室を一対又は複数対設け、この装
置本体内又は装置本体の排出口後方に吸引装置を設けた
ことを特徴とする、無電界エアークリーン装置。6. A mixing chamber for mixing steam formed by heating water is provided in a chamber following an air insertion port of a hollow apparatus main body, and water droplets or particles in the air are mixed with the air after the mixing chamber. A non-electric field characterized by providing a particle separation device chamber for separation, providing one or more pairs of the mixing chamber and the particle separation device room, and providing a suction device in the device main body or behind the outlet of the device main body. Air clean equipment.
部屋に水を噴霧するノズルを設け、この噴霧室につづ
き、エアーのなかの水滴又は粒子をエアーと分離する粒
子分離装置室を設け、この粒子分離装置室にはエアーの
流通方向と平行に複数枚の板体を相互に間隔をあけて相
対向して並べ設け、これらの各板体の間隔を二層流が生
じる巾とし、これらの噴霧室及び粒子分離装置室を一対
又は複数対設け、この装置本体内又は装置本体の排出口
後方に吸引装置を設けたことを特徴とする、無電界エア
ークリーン装置。7. A nozzle for spraying water is provided in a chamber following the air insertion port of the hollow apparatus main body, and a particle separation apparatus chamber for separating water droplets or particles in the air from the air is provided following the spray chamber. In this particle separation device chamber, a plurality of plates are arranged in parallel with each other at an interval in parallel with the air flow direction, and the interval between these plates is set to a width at which a two-layer flow is generated. A plurality of spray chambers and a plurality of particle separation apparatus chambers, and a suction device provided in the apparatus main body or behind the outlet of the apparatus main body.
部屋に、水を加熱して成る蒸気とエアーを混合する混合
室を設け、この混合室につづき、エアーのなかの水滴又
は粒子をエアーと分離する粒子分離装置室を設け、この
粒子分離装置室にはエアーの流通方向と平行に複数枚の
板体を相互に間隔をあけて相対向して並べ設け、これら
の各板体の間隔を二層流が生じる巾とし、これらの混合
室及び粒子分離装置室を一対又は複数対設け、この装置
本体内又は装置本体の排出口後方に吸引装置を設けたこ
とを特徴とする、無電界エアークリーン装置。8. A mixing chamber for mixing steam and air formed by heating water is provided in a chamber following an air insertion port of a hollow apparatus main body. After the mixing chamber, water droplets or particles in the air are removed from the air. A plurality of plate bodies are arranged in parallel in the direction of air flow in the particle separation apparatus room so as to face each other with an interval therebetween. A width in which a two-layer flow is generated, a pair or a plurality of pairs of the mixing chamber and the particle separation apparatus chamber, and a suction device provided in the apparatus main body or behind the discharge port of the apparatus main body. Air clean equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09156100A JP3108867B2 (en) | 1997-05-30 | 1997-05-30 | Electric field-free air cleaning method and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09156100A JP3108867B2 (en) | 1997-05-30 | 1997-05-30 | Electric field-free air cleaning method and apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH10328519A true JPH10328519A (en) | 1998-12-15 |
| JP3108867B2 JP3108867B2 (en) | 2000-11-13 |
Family
ID=15620319
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP09156100A Expired - Fee Related JP3108867B2 (en) | 1997-05-30 | 1997-05-30 | Electric field-free air cleaning method and apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3108867B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018030090A (en) * | 2016-08-24 | 2018-03-01 | 三菱日立パワーシステムズ環境ソリューション株式会社 | Particle removal device |
| CN108981030A (en) * | 2018-07-04 | 2018-12-11 | 湖州知辉进出口贸易有限公司 | A kind of air cleaning unit of circulation cyclone dust removal |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR102018384B1 (en) * | 2018-02-13 | 2019-09-04 | 부산대학교 산학협력단 | Air cleaner for room |
-
1997
- 1997-05-30 JP JP09156100A patent/JP3108867B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018030090A (en) * | 2016-08-24 | 2018-03-01 | 三菱日立パワーシステムズ環境ソリューション株式会社 | Particle removal device |
| CN108981030A (en) * | 2018-07-04 | 2018-12-11 | 湖州知辉进出口贸易有限公司 | A kind of air cleaning unit of circulation cyclone dust removal |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3108867B2 (en) | 2000-11-13 |
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| Date | Code | Title | Description |
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| LAPS | Cancellation because of no payment of annual fees |