JPH0577466B2 - - Google Patents
Info
- Publication number
- JPH0577466B2 JPH0577466B2 JP60207767A JP20776785A JPH0577466B2 JP H0577466 B2 JPH0577466 B2 JP H0577466B2 JP 60207767 A JP60207767 A JP 60207767A JP 20776785 A JP20776785 A JP 20776785A JP H0577466 B2 JPH0577466 B2 JP H0577466B2
- Authority
- JP
- Japan
- Prior art keywords
- air
- water
- water droplets
- million
- ultra
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F6/00—Air-humidification, e.g. cooling by humidification
- F24F6/12—Air-humidification, e.g. cooling by humidification by forming water dispersions in the air
- F24F6/14—Air-humidification, e.g. cooling by humidification by forming water dispersions in the air using nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/02—Cleaning by the force of jets or sprays
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto
- B08B9/08—Cleaning containers, e.g. tanks
- B08B9/093—Cleaning containers, e.g. tanks by the force of jets or sprays
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/54—Free-cooling systems
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Combustion & Propulsion (AREA)
- General Engineering & Computer Science (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Of Particles Using Liquids (AREA)
- Nozzles (AREA)
- Air Humidification (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Detergent Compositions (AREA)
- Glanulating (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、空気1立方メートル当り7063万個以
上、好ましくは17657万個以上、より好ましくは
35314万個以上含有させる超微細水滴の製造方法
に関するものでる。[Detailed Description of the Invention] [Industrial Application Field] The present invention provides at least 70.63 million particles per cubic meter of air, preferably at least 176.57 million particles, more preferably at least 176.57 million particles per cubic meter of air.
This paper relates to a method for producing ultrafine water droplets containing 353.14 million or more.
病院、薬品製造工場、食品製造工場、食品冷蔵
室、研究所、実験室等では塵埃や微生物を含まな
い清浄気体が必要であり、そのためにはエアーフ
イルターを用いて清浄化した空気を送気したり、
出入口部にエアーカーテンを設置したりする方策
が採られている。
Hospitals, drug manufacturing plants, food manufacturing plants, food refrigerated rooms, laboratories, laboratories, etc. require clean gas that does not contain dust or microorganisms, and for this purpose air filters are used to supply purified air. Or,
Measures such as installing air curtains at entrances and exits are being taken.
しかしながら、上記のような方法は充分に清浄
化された気体を得ることはできないし、エアーシ
ヤワールームを利用しても充分に目的を達成する
ことはできない。更に、LSI、超LSI製造工場、
生物製剤製造工場、手術室、精密機械の洗浄工
場、無菌食品製造工場、冷蔵室等のように、細菌
やウイルスの混入はおろか0.5μ以下の塵埃の混入
も許されない厳格な条件のもとで、超クリーンな
清浄気体を工業的規模で送入することは、現在で
は不可能とされている。
However, the above method cannot obtain sufficiently purified gas, and even if an air shower room is used, the purpose cannot be fully achieved. Furthermore, LSI, super LSI manufacturing factories,
Under strict conditions such as biological drug manufacturing factories, operating rooms, precision machinery cleaning factories, sterile food manufacturing factories, refrigerator rooms, etc., where not only bacteria and viruses but also dust of 0.5μ or less are not allowed to enter. It is currently impossible to deliver ultra-clean gas on an industrial scale.
そこで、このような高度に清浄化された冷蔵室
や、室や工場を得ることは各種の業界において広
く切望されており、本発明はこのような時代の要
請に応えるべくなされたものである。 Therefore, it is widely desired in various industries to obtain such a highly purified refrigerating room, room, or factory, and the present invention was made to meet the demands of this era.
本出願人は、超クリーンな清浄気体を工業的規
模で得ることに関し、鋭意研究を行なつたとこ
ろ、空気に混入した水滴が空気中に混在する塵埃
を吸着して空気を清浄化するという現象に着目
し、更に水滴の粒子を小さくして実質的に0.5ミ
クロン以下の超微細水滴にして空気1立方メート
ル当り7063万個以上、好ましくは17657万個以上、
より好ましくは35314万個以上含有させて送気す
れば、空気中の微細な塵埃はもちろんこと細菌、
糸状菌、胞子類はおろかウイルスまでもこれらを
付着して清浄化、除菌することができることが判
明した。そして、このような超微細水滴を浮遊せ
しめた気体雰囲気では、該雰囲気を清浄化できる
のみでなく、全く予期せざることに、超微細水滴
の場合は水滴が存在するにもかかわらず物体がぬ
れるという現象が生じないという顕著な効果が奏
されることをつきとめた。そして更に検討した結
果、微細水滴浮遊気体雰囲気中に通常の気体を通
したところ、該通常気体が超クリーンな状態にま
で高度に清浄化され、このように高度に清浄化さ
れた気体をそれぞれの部屋、部署、その他関係個
所に直接適用できることも見出した。
The applicant has conducted extensive research into obtaining ultra-clean clean gas on an industrial scale, and discovered a phenomenon in which water droplets mixed in the air purify the air by adsorbing dust mixed in the air. Focusing on this, the water droplets are further reduced to ultra-fine water droplets of substantially 0.5 microns or less, at least 70.63 million, preferably at least 176.57 million, per cubic meter of air.
More preferably, if the air is supplied with at least 353,140,000 particles, not only fine dust particles in the air but also bacteria,
It has been found that it is possible to attach not only filamentous fungi and spores but also viruses to clean and sterilize them. In a gaseous atmosphere in which such ultrafine water droplets are suspended, not only can the atmosphere be purified, but also, quite unexpectedly, objects can become wet despite the presence of ultrafine water droplets. It has been found that this phenomenon has a remarkable effect in that this phenomenon does not occur. As a result of further investigation, we found that when normal gas was passed through a gas atmosphere containing suspended fine water droplets, the normal gas was highly purified to an ultra-clean state. We also found that it can be applied directly to rooms, departments, and other related areas.
本発明は、水噴射装置内の噴射管に多数設けら
れた直径0.2〜8mm、好ましくは0.5〜3mmのノズ
ルからゲージ圧0.3〜5.5Kg/cm2、好ましくは0.5〜
2.5Kg/cm2で水を噴射させ、ノズルから10〜150cm
はなれた側部に衝突させてきわめて多数の超微細
水滴を発生させ、ここに空気を風速15〜50m/
sec、風量3〜3000m3/minの条件で送り、粒径
0.5ミクロン以下の超微細水滴を1立方メートル
当り7063万個以上、好ましくは17657万個以上、
より好ましくは35314万個以上含有する空気を得
ることを特徴とする超微細水滴の製造方法であ
る。 The present invention provides a gauge pressure of 0.3 to 5.5 Kg/cm 2 , preferably 0.5 to 5.0 kg/cm 2 , from a number of nozzles with a diameter of 0.2 to 8 mm, preferably 0.5 to 3 mm, provided in an injection pipe in a water injection device.
Spray water at 2.5Kg/ cm2 , 10-150cm from the nozzle.
A very large number of ultra-fine water droplets are generated by colliding with the separated side, and the air is blown here at a wind speed of 15 to 50 m/s.
sec, air volume 3-3000m3 /min, particle size
Ultrafine water droplets of 0.5 microns or less per cubic meter of 70.63 million or more, preferably 176.57 million or more,
More preferably, the method for producing ultrafine water droplets is characterized by obtaining air containing 353.14 million or more.
本発明においては、水噴射装置内の噴射管には
多数の、例えば30ケ〜1500ケの直径0.2〜8mm、
好ましくは0.5〜3mmのノズルが設けられる。水
は高い圧力でポンプによつて送られ、ゲージ圧
0.3〜5.5Kg/cm2、好ましくは0.5〜2..5Kg/cm2で水
を各ノズルから噴射させるが水の量は1ケのノズ
ル当り1〜3/分もの大量の水が噴射される。
水はノズルから10〜150cmはなれた側壁に衝突さ
せてきわめて多数の超微細水滴を発生させるが、
ここに空気を風速15〜50m/sec程度で風量3〜
3000m3/minの目安で送り込み、粒径0.5ミクロ
ン以下の超微細水滴を1立方メートル当り7063万
個以上、好ましくは17657万個以上、より好まし
くは35314万個以上含有する空気を得るものであ
る。
In the present invention, the injection pipe in the water injection device has a large number of, for example, 30 to 1500 pieces with a diameter of 0.2 to 8 mm,
Preferably a 0.5-3 mm nozzle is provided. Water is pumped at high pressure, gauge pressure
Water is injected from each nozzle at 0.3 to 5.5 Kg/cm 2 , preferably 0.5 to 2.5 Kg/cm 2 , and a large amount of water is injected from 1 to 3 minutes per nozzle. .
The water collides with the side wall 10 to 150 cm away from the nozzle, generating an extremely large number of ultra-fine water droplets.
Air is pumped here at a wind speed of 15 to 50 m/sec and a flow rate of 3 to 50 m/sec.
The air is fed at a rate of 3000 m 3 /min to obtain air containing 70.63 million or more, preferably 176.57 million or more, more preferably 353.14 million or more ultrafine water droplets with a particle size of 0.5 microns or less per cubic meter.
次に、本発明方法を実施するための装置の数例
を図示した図面を参照しながら、本発明方法を詳
述する。
The method of the invention will now be described in detail with reference to the drawings, which illustrate some examples of apparatus for carrying out the method of the invention.
先ず第1図を参照されたい。この装置は、本発
明を実施するための最も基礎的なものであつて、
水噴射装置1の壁近くに噴射管2を設け、これに
は多数の水噴射ノズル3を設ける。これらのノズ
ル3は、対向する側面に設けたノズルの位置とは
少しずらして交互に配置し、相対するノズルを直
線上に配置しないようにするのが良い。ノズルは
30ケ〜1500ケ設けられ、直径は0.2〜8mm、好ま
しくは0.5〜3mmで、水はゲージ圧0.3〜5.5Kg/
cm2、好ましくは0.5〜2.5Kg/cm2で10〜150cmはな
れた向うの壁に噴射される。 Please refer to FIG. 1 first. This device is the most basic device for implementing the present invention, and
An injection pipe 2 is provided near the wall of a water injection device 1, and a large number of water injection nozzles 3 are provided therein. It is preferable that these nozzles 3 are arranged alternately so as to be slightly shifted from the positions of the nozzles provided on the opposing sides, so that the opposing nozzles are not arranged on a straight line. The nozzle is
There are 30 to 1500 pieces, the diameter is 0.2 to 8 mm, preferably 0.5 to 3 mm, and the water gauge pressure is 0.3 to 5.5 kg/
cm 2 , preferably 0.5 to 2.5 Kg/cm 2 , is sprayed onto the opposite wall at a distance of 10 to 150 cm.
噴射された水は、対向する側面に衝突して超微
細水滴となり、水噴射装置1内はこの超微細水滴
で充満される。水噴射装置1内には送入口4から
空気を風速15〜50m/sec程度で、風量3〜3000
m3/min程度で送り込み、粒径0.5ミクロン以下
の超微細水滴を1立方メートル当り7063万個以
上、好ましくは17657万個以上、より好ましくは
35314万個以上含有する空気とし、これを送出口
5から取出す。送出口5を出た超微細水滴を含む
空気は大きな水滴を含むことがあるので、サイク
ロン6の接線方向入口7からサイクロン6に送入
し、大きな水滴を除去して送気管8から取り出す
ものである。取り出された超微細水滴を含む空気
はそれぞれの室に送つて、水噴射装置に帰し、循
環させるものである。 The jetted water collides with the opposing side surfaces and becomes ultrafine water droplets, and the inside of the water injection device 1 is filled with these ultrafine water droplets. Air is supplied into the water injection device 1 from the inlet 4 at a wind speed of about 15 to 50 m/sec, with an air volume of 3 to 3000.
The ultrafine water droplets with a particle size of 0.5 microns or less are fed at a rate of about m 3 /min, and 70.63 million or more, preferably 176.57 million or more, and more preferably 176.57 million or more per cubic meter.
The air contains 353,140,000 or more particles, and is taken out from the outlet 5. Since the air containing ultrafine water droplets leaving the outlet 5 may contain large water droplets, it is fed into the cyclone 6 from the tangential inlet 7 of the cyclone 6, large water droplets are removed, and the air is taken out from the air pipe 8. be. The extracted air containing ultrafine water droplets is sent to each chamber, returned to the water injection device, and circulated.
第4図乃至第9図は、更に効率よく、しかも温
度コントロールした超微細水滴浮遊気体を製造す
るための装置である。 FIGS. 4 to 9 show an apparatus for producing gas suspended in ultrafine water droplets more efficiently and with temperature control.
水噴射装置40の円筒部41内には、冷凍装置
の蒸発管47が配置されている。蒸発管47とノ
ズル45の位置関係は、相互に完全にずらしても
よいし、また少しずらしてもよく、また噴射ノズ
ル45からの水が蒸発管47に対して垂直に噴射
状態で吹き付けられるように配置されている。ノ
ズルは30ケ〜1500ケ程度設けられ、直径は0.2〜
8mm、好ましくは0.5〜3mmで、水はゲージ圧0.3
〜5.5Kg/cm2、好ましくは0.5〜2.5Kg/cm2で、水の
量は1ケのノズル当り1〜3/分の量で噴射さ
れる。ノズルから側壁までは10〜150cmはなして
設けられる。水噴射装置の円錐部51の下端部に
は、濾過装置48、水タンク48、ポンプ50が
順次設けられている。従つて、冷水は矢印Bの方
向、すなわちポンプ50、循環管45、噴射管4
4、水噴射器の円筒部41、円錐部51、濾過装
置48、水タンク49、ポンプ50の順序で循環
させられる。冷媒、特に高温冷媒(1℃−5℃)
は、矢印Cの方向に蒸発管47内を循環する。空
気は、矢印Aの方向にしたがつて入口42を通つ
て水噴射装置内に送り込まれ、水噴射装置内で微
細水滴を含有すると同時に冷却されて目的とする
空気となり、出口管43を通つてそれぞれの目的
に使用される。噴射管44に設けたノズル45か
らゲージ圧0.3〜5.5Kg/cm2、好ましくは0.5〜2.5
Kg/cm2で水を噴射させ、ノズルから10〜150cmは
なれた冷凍装置の蒸発管47及び/又は円筒部4
1の側壁に衝突せしめると(E)、超微細水滴が
発生し(それとともに、蒸発管47と衝突した水
流はこの管47内を通る冷媒と熱交換を行い、冷
却される)、且つ水滴は冷却される。このような
雰囲気中空気を風速15〜50m/sec程度で風量3
〜3000m3/minの目安で矢印Aにしたがつて通過
せしめると、この空気は超微細水滴を含有すると
ともに冷却された水滴と熱交換を行つてそれ自体
は冷却され、0.5ミクロン以下の超微細水滴を1
立方メートル当り7063万個以上、好ましくは
17657万個以上、より好ましくは35314万個以上含
有する空気とするものである。この際、空気の循
環による遠心作用により実質的に0.5ミクロンよ
り大きいものは分離されている。必要によつて
は、サイクロンで除水滴することもできる。 In the cylindrical portion 41 of the water injection device 40, an evaporation pipe 47 of the refrigeration device is arranged. The positional relationship between the evaporation pipe 47 and the nozzle 45 may be completely shifted from each other, or may be slightly shifted from each other, and the water from the injection nozzle 45 may be sprayed perpendicularly to the evaporation pipe 47 in a spray state. It is located in Approximately 30 to 1500 nozzles are provided, and the diameter is 0.2 to 1,500.
8mm, preferably 0.5-3mm, water at gauge pressure 0.3
~5.5Kg/ cm2 , preferably 0.5-2.5Kg/ cm2 , and the amount of water is injected at a rate of 1-3/min per nozzle. The distance from the nozzle to the side wall is 10 to 150 cm. A filtration device 48, a water tank 48, and a pump 50 are sequentially provided at the lower end of the conical portion 51 of the water injection device. Therefore, the cold water flows in the direction of arrow B, that is, the pump 50, the circulation pipe 45, and the injection pipe 4.
4. The water is circulated in the order of the cylindrical part 41, conical part 51, filtration device 48, water tank 49, and pump 50 of the water injector. Refrigerants, especially high temperature refrigerants (1℃-5℃)
circulates within the evaporation tube 47 in the direction of arrow C. The air is fed into the water injection device through the inlet 42 according to the direction of arrow A, contains fine water droplets in the water injection device, is simultaneously cooled and becomes the desired air, and is then passed through the outlet pipe 43. used for their respective purposes. A gauge pressure of 0.3 to 5.5 Kg/cm 2 , preferably 0.5 to 2.5 is applied from the nozzle 45 provided in the injection pipe 44.
The evaporator tube 47 and/or the cylindrical part 4 of the refrigeration device is 10 to 150 cm away from the nozzle and injects water at Kg/cm 2 .
1 (E), ultrafine water droplets are generated (at the same time, the water flow that collided with the evaporation tube 47 exchanges heat with the refrigerant passing through this tube 47 and is cooled), and the water droplets cooled down. The air in such an atmosphere is blown at a wind speed of 15 to 50 m/sec and the air volume is 3.
When the air is allowed to pass according to arrow A at a rate of ~3000m 3 /min, it contains ultrafine water droplets and exchanges heat with the cooled water droplets to cool itself, resulting in ultrafine particles of 0.5 microns or less. 1 drop of water
70.63 million pieces per cubic meter or more, preferably
The air contains 176.57 million or more, more preferably 353.14 million or more. At this time, particles larger than 0.5 microns are substantially separated by centrifugal action due to air circulation. If necessary, water can be removed using a cyclone.
第7図は、本発明方法を64キロビツトRAM量
産工場に対して実際に適用するためのトータルシ
ステムを示した模式図である。上述したところに
したがつて、水噴射装置40で製造された超微細
水滴浮遊空気は、矢印Aにしたがつて除滴サイク
ロン50に送り込まれる。すなわち40から出て
きた気体は、除滴サイクロン50の側壁に接線方
向に設けた入口からサイクロン内部に入り、この
中を循環している間に余分の水滴、大きな水滴を
除去して0.5μ以下の超微細水滴を90%以上浮遊せ
しめた気体に調製して、サイクロン50の中央部
に設けた出口管からこれを取り出す。 FIG. 7 is a schematic diagram showing a total system for actually applying the method of the present invention to a 64 kilobit RAM mass production factory. According to the above-described process, the ultrafine water droplets suspended in the air produced by the water injection device 40 are fed into the drip removal cyclone 50 in the direction of arrow A. In other words, the gas coming out of the drip removing cyclone 50 enters the inside of the cyclone through an inlet provided tangentially to the side wall of the cyclone 50, and while circulating inside the cyclone, excess water droplets and large water droplets are removed and reduced to 0.5μ or less. A gas in which 90% or more of ultrafine water droplets are suspended is prepared and taken out from an outlet pipe provided in the center of the cyclone 50.
このようにして取り出された超微細水滴浮遊空
気は、実質的に0.5ミクロンより大きいものを除
くためにフイルターFを有するパイプPを通つて
エアーシヤワールーム60に送られて、更には隣
接する超クリーンルーム70で作業をする人々の
洗浄を行う。また上記超微細水滴浮遊空気の一部
は、直接超クリーンルーム70に送られて、室内
に塵埃を含まない清浄化した空気を送入するとと
もにLSIに用いるシリコン板の洗浄にもこれを使
用する。超クリーンルーム70で使用された空気
は、そこから取り出し、パイプP、フアンFを介
して水噴射装置40へ戻し、このサイクルをくり
返すのである。この方法によれば、超クリーンル
ーム内には1立方メートルの空間に0.5μ以上の塵
はわずか35個未満しかないという超クリーンな状
態に保たれていることが判明した。ちなみに、通
常の工場では数万個の塵埃が浮遊しており、この
ことからも、本発明による方法がいかにすぐれて
いるかが判るはずである。 The ultrafine water droplets suspended in the air taken out in this way are sent to the air shower room 60 through a pipe P having a filter F to remove particles substantially larger than 0.5 microns, and further to the adjacent ultra clean room. 70 to clean the people working there. Further, a part of the air floating in ultra-fine water droplets is directly sent to the ultra-clean room 70 to introduce clean air that does not contain dust into the room, and is also used to clean silicon plates used in LSIs. The air used in the super clean room 70 is taken out from there and returned to the water injection device 40 via the pipe P and fan F, and this cycle is repeated. Using this method, it was found that the ultra-clean room was maintained in an ultra-clean state with less than 35 pieces of dust larger than 0.5 micrometers per cubic meter of space. Incidentally, tens of thousands of pieces of dust are floating in a typical factory, and this fact should show how superior the method according to the present invention is.
また、第8図及び第9図に示されるように、除
滴サイクロン50の次に熱交換器100を設け、
これに超微細水滴浮遊気体を通すことによつて、
空気を最適温度させることができるものである。
熱交換器100は次に説明される。即ち、缶体1
01の中心部には空気排出管105を上下方向に
設けてあり、管体101外に設けた空気導管10
5′と連通する。従つて、空気取入管104より
の空気は缶体101内を旋回しながら下方に達し
空気排出管105の下部より上昇して矢印方向に
移動することになる。又缶体101の内部には外
側配管106及び内側配管107を設けてあり、
各配管106,107の下端は缶体101外に設
けたポンプ108と連通し、温水又は冷水を流通
させ上部排水口109,110より排水させられ
る。缶体101の上部及び下部には洗浄水管11
1の水噴射出口111a,111b……を多数設
けてあり、配管106及び配管107の上下列の
上方又は下方に望ませ、配管106,107及び
缶体101の内面、空気排出管105の外面に向
けて洗浄水を噴出できるようにしてある。またコ
ーン部102の下方には、排水管112′が設け
られており、缶内の洗浄水又は気体冷却によるド
レイン等が排出できるようにしてある。従つて空
気取入口104より空気は缶体101内でサイク
ロン効果によりごみ等を分離し、配管106,1
07により適温に加熱又は冷却され、適温となつ
た空気は空気排出管105により送出される。又
分離したごみ等は洗浄水管111に通水し、ノズ
ル111a,111b……より噴水させることに
よりより洗い去ることができるものである。 Further, as shown in FIGS. 8 and 9, a heat exchanger 100 is provided next to the drip removal cyclone 50,
By passing ultrafine water droplets suspended gas through this,
It can bring the air to the optimum temperature.
Heat exchanger 100 will now be described. That is, can body 1
An air discharge pipe 105 is provided in the center of the pipe body 101 in the vertical direction, and an air conduit pipe 10 provided outside the pipe body 101
It communicates with 5'. Therefore, the air from the air intake pipe 104 reaches the bottom while swirling inside the can body 101, rises from the lower part of the air discharge pipe 105, and moves in the direction of the arrow. Furthermore, an outer pipe 106 and an inner pipe 107 are provided inside the can body 101.
The lower end of each pipe 106, 107 communicates with a pump 108 provided outside the can body 101, and hot or cold water is passed through and drained from upper drain ports 109, 110. Washing water pipes 11 are installed at the upper and lower parts of the can body 101.
A large number of water injection outlets 111a, 111b, etc. are provided, and are arranged above or below the upper and lower rows of pipes 106 and 107. It is designed so that cleaning water can be sprayed towards it. Further, a drain pipe 112' is provided below the cone portion 102 so that cleaning water or drain from gas cooling inside the can can be discharged. Therefore, the air from the air intake port 104 separates dust etc. in the can body 101 by the cyclone effect, and then flows into the pipes 106, 1.
The air that has been heated or cooled to an appropriate temperature by 07 is sent out through an air discharge pipe 105. Further, the separated dust can be further washed away by passing water through the washing water pipe 111 and spraying water from the nozzles 111a, 111b, . . . .
このように処理された空気はほぼ完全に0.5ミ
クロン以下の超微細水滴を多量浮遊した状態とな
つているので、これを用いて室内を処理すること
によつてあらゆる物を清浄化することができるの
である。 The air treated in this way is almost completely made up of a large amount of ultra-fine water droplets of 0.5 microns or less suspended, so by treating the room with these, you can clean everything. It is.
本発明方法において使用する0.5ミクロン以下
の超微細水滴は表面張力がきわめて低く、物体に
附着したり、空中に浮遊している塵埃に超微細水
滴が容易に付着し、更にこの超微細水滴が互いに
集合し、大きくなり顕著に質量がふえ送風ととも
に塵埃は除去される。特に、本法によれば超微細
水滴を使用するために、非常に微細な塵埃のみで
はなく、細菌やウイルスまでも除去することがで
き、物理的にも生物的にも室内は清浄化されると
いう著効が奏される。ウイルスは、従来エアーフ
イルタ等で除去していたのであるが、ウイルスは
ずか0.5μ〜0.01μの大きさしかないため、エアー
フイルタでは充分除去することが不可能であつ
た。したがつて、本発明で室内を清浄化すれば現
実に風をひくといつたことも非常に少なくなり、
病院、薬局、研究室、産院等に使用するのに極め
て好適である。
The surface tension of the ultra-fine water droplets of 0.5 microns or less used in the method of the present invention is extremely low, and the ultra-fine water droplets easily attach to objects or dust floating in the air, and furthermore, these ultra-fine water droplets can interact with each other. The dust gathers, becomes larger, noticeably increases in mass, and is removed along with the air blowing. In particular, since this method uses ultra-fine water droplets, it is possible to remove not only extremely fine dust but also bacteria and viruses, cleaning the room both physically and biologically. This effect is achieved. Viruses have conventionally been removed using air filters, but since viruses are only 0.5 to 0.01 microns in size, it has been impossible to remove them sufficiently with air filters. Therefore, if you use the present invention to clean your room, you will be much less likely to actually experience a draft.
It is extremely suitable for use in hospitals, pharmacies, laboratories, maternity hospitals, etc.
また、本発明方法は雑菌を含まなくすることが
できる特色の故に、食品製造工場において、食品
の洗浄、装置の洗浄に使用することができ、例え
ば冷凍肉に解凍、サラダや野菜、鮮魚、精肉の保
存等食料品店、スーパーマーケツトその他で使用
するものにも極めて好適であるし、特に雑菌混入
の危険性があるためにその製造に制約があつた生
ハムも自由に製造することができる。 In addition, because the method of the present invention has the feature of being free of germs, it can be used in food manufacturing factories for cleaning food and cleaning equipment, such as thawing frozen meat, salads, vegetables, fresh fish, and meat. It is also extremely suitable for use in food stores, supermarkets, etc., such as preservation of raw ham, and can also freely produce raw ham, which has been subject to restrictions due to the risk of contamination with bacteria.
第1図は、超微細水滴の製造装置の1実施例を
図示したものであり、第2図は第1図の装置の中
央部を切断したときの断面図であり、第3図は、
除水滴のサイクロンであり、第4図は、超微細水
滴製造装置の別の装置を図示したものであり、第
5図は第4図の装置の上部横断面図であり、第6
図は第4図の装置の中央部を切断したときの断面
図であり、そして第7図は、実際の半導体製造工
場において適用した場合のトータルシステムを模
式的に図示したものである。また、第8図は超微
細水滴製造装置のあとにつけることのできる熱交
換器を示す図で、第9図はその上部横断面図であ
る。
1,40……水噴射装置、3,45……ノズ
ル、43……超微細水滴浮遊気体出口管、50…
…除滴サイクロン、60……エアーシヤワールー
ム、70……超クリーンルーム、100……熱交
換器。
FIG. 1 shows an embodiment of an apparatus for producing ultra-fine water droplets, FIG. 2 is a sectional view taken through the center of the apparatus shown in FIG. 1, and FIG.
4 is a cyclone of water removal droplets, FIG. 4 is a diagram illustrating another device for producing ultra-fine water droplets, FIG. 5 is a cross-sectional view of the upper part of the device in FIG. 4, and FIG.
This figure is a sectional view taken through the center of the apparatus shown in FIG. 4, and FIG. 7 schematically shows the total system when applied in an actual semiconductor manufacturing factory. Moreover, FIG. 8 is a diagram showing a heat exchanger that can be attached after the ultrafine water droplet production apparatus, and FIG. 9 is a cross-sectional view of the upper part thereof. 1,40...Water injection device, 3,45...Nozzle, 43...Ultrafine water droplet suspended gas outlet pipe, 50...
...Drop removal cyclone, 60...Air shower room, 70...Super clean room, 100...Heat exchanger.
Claims (1)
0.2〜8mm、好ましくは0.5〜3mmのノズルからゲ
ージ圧0.3〜5.5Kg/cm2、好ましくは0.5〜2.5Kg/
cm2で水を噴射させ、ノズルから10〜150cmはなれ
た側部に衝突させてきわめて多数の超微細水滴を
発生させ、ここに空気を風速15〜50m/sec、風
量3〜3000m3/minの条件で送り、粒径0.5ミク
ロン以下の超微細水滴を1立方メートル当り7063
万個以上、好ましくは17657万個以上、より好ま
しくは35314万個以上含有する空気を得ることを
特徴とする超微細水滴の製造方法。1. Diameters of multiple injection pipes in a water injection device
A gauge pressure of 0.3 to 5.5 Kg/cm 2 , preferably 0.5 to 2.5 Kg/cm 2 from a 0.2 to 8 mm, preferably 0.5 to 3 mm nozzle.
cm 2 and collides with the side 10 to 150 cm away from the nozzle to generate an extremely large number of ultra-fine water droplets. 7063 ultra-fine water droplets with a particle size of 0.5 microns or less per cubic meter
A method for producing ultrafine water droplets, characterized by obtaining air containing 10,000 or more, preferably 176.57 million or more, more preferably 353.14 million or more.
Priority Applications (16)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60207767A JPS6268515A (en) | 1985-09-21 | 1985-09-21 | Method for producing ultrafine water droplets |
| SE8603728A SE8603728L (en) | 1985-09-21 | 1986-09-05 | SET FOR PREPARING A SUSPENSION IN AIR OF ULTRAPHINE DIMP PARTICLES |
| DK426086A DK426086A (en) | 1985-09-21 | 1986-09-05 | PROCEDURE FOR KEEPING ULTRAFINE TEMPERATURES SOILING IN AIR |
| IN723/MAS/86A IN168582B (en) | 1985-09-21 | 1986-09-09 | |
| AU62505/86A AU577203B2 (en) | 1985-09-21 | 1986-09-09 | Producing suspension of ultra-fine mist particles |
| CA000517874A CA1265435A (en) | 1985-09-21 | 1986-09-10 | Method for producing suspension in air of ultra-fine mist particles |
| IT48442/86A IT1196617B (en) | 1985-09-21 | 1986-09-11 | METHOD TO PRODUCE A SUSPENSION IN THE AIR OF ULTRAFINE PARTS OF MIST, IN PARTICULAR TO CLEAN AN ENVIRONMENT |
| FR868612689A FR2587628B1 (en) | 1985-09-21 | 1986-09-11 | PROCESS FOR THE PRODUCTION OF A SUSPENSION OF ULTRAFINE WATER PARTICLES IN THE AIR |
| NL8602323A NL8602323A (en) | 1985-09-21 | 1986-09-15 | METHOD FOR PREPARING A SUSPENSION OF ULTRA-FINE AEROUS MICRODROPS IN AIR AND METHOD FOR CLEANING THE INTERIOR OF A ROOM. |
| GB8622410A GB2180776B (en) | 1985-09-21 | 1986-09-17 | Method for producing suspension in air of ultra-fine mist particles |
| KR1019860007837A KR910005982B1 (en) | 1985-09-21 | 1986-09-17 | Manufacturing method of micro-droplet floating air and indoor cleaning method |
| BR8604462A BR8604462A (en) | 1985-09-21 | 1986-09-17 | PROCESSES TO PRODUCE AN AIR SUSPENSION OF ULTRA-THIN WATER MICRO-DROPS AND TO CLEAN THE INSIDE OF AN ENCLOSURE |
| ES8602023A ES2002360A6 (en) | 1985-09-21 | 1986-09-19 | Forming mist of ultra-fine water particles in air - by spraying in specific conditions from multiple nozzles |
| DE19863631926 DE3631926A1 (en) | 1985-09-21 | 1986-09-19 | METHOD FOR PRODUCING A FOG OF VERY FINE HUMIDITY PARTICLES IN AIR |
| CH3764/86A CH669834A5 (en) | 1985-09-21 | 1986-09-19 | |
| CN86106342.2A CN1004860B (en) | 1985-09-21 | 1986-09-20 | Method for producing suspension in air of ultra-fine mist particles |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60207767A JPS6268515A (en) | 1985-09-21 | 1985-09-21 | Method for producing ultrafine water droplets |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6268515A JPS6268515A (en) | 1987-03-28 |
| JPH0577466B2 true JPH0577466B2 (en) | 1993-10-26 |
Family
ID=16545195
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60207767A Granted JPS6268515A (en) | 1985-09-21 | 1985-09-21 | Method for producing ultrafine water droplets |
Country Status (15)
| Country | Link |
|---|---|
| JP (1) | JPS6268515A (en) |
| KR (1) | KR910005982B1 (en) |
| CN (1) | CN1004860B (en) |
| AU (1) | AU577203B2 (en) |
| BR (1) | BR8604462A (en) |
| CA (1) | CA1265435A (en) |
| CH (1) | CH669834A5 (en) |
| DE (1) | DE3631926A1 (en) |
| DK (1) | DK426086A (en) |
| FR (1) | FR2587628B1 (en) |
| GB (1) | GB2180776B (en) |
| IN (1) | IN168582B (en) |
| IT (1) | IT1196617B (en) |
| NL (1) | NL8602323A (en) |
| SE (1) | SE8603728L (en) |
Families Citing this family (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2698160B1 (en) * | 1992-11-13 | 1994-12-23 | France Grignotage | Method and device for the treatment of working atmospheres using a cyclonic exchanger. |
| DE29821687U1 (en) * | 1998-12-05 | 2000-04-06 | GEA Finnah GmbH, 48683 Ahaus | Device for producing an aerosol |
| IT1303661B1 (en) * | 1998-12-24 | 2001-02-21 | Tecmeco S R L | WATER NEBULIZATION AIR CLEANER |
| DE10024889B4 (en) * | 2000-05-16 | 2008-09-04 | Gea Wtt Gmbh | Plate heat exchanger with atomizer |
| US7008535B1 (en) * | 2000-08-04 | 2006-03-07 | Wayne State University | Apparatus for oxygenating wastewater |
| DE10062630A1 (en) * | 2000-12-15 | 2002-08-29 | Bartels Mikrotechnik Gmbh | Beduftungsverfahren |
| KR100509012B1 (en) * | 2002-12-13 | 2005-08-19 | 조인섭 | Dispersal air scrubber and method thereof |
| KR101445703B1 (en) * | 2012-06-18 | 2014-09-29 | 주식회사 포스코 | The noxious gas of dust purification apparatus |
| CN104096432B (en) * | 2013-04-12 | 2016-12-28 | 张灵样 | Mist dust remover |
| CN104368465A (en) * | 2013-08-13 | 2015-02-25 | 宁夏嘉翔自控技术有限公司 | Asphalt melting Venturi spraying dust removing nozzle |
| KR101565761B1 (en) * | 2014-11-24 | 2015-11-04 | 오홍근 | Filtration system |
| DE102016200894A1 (en) * | 2016-01-22 | 2017-07-27 | Olympus Winter & Ibe Gmbh | Medical flue gas cleaning apparatus and method for cleaning medical flue gases |
| CN107314449B (en) * | 2017-08-18 | 2023-07-28 | 广东美的制冷设备有限公司 | Air treatment module and air conditioner |
| KR102054253B1 (en) * | 2019-04-16 | 2019-12-10 | 주식회사 넥스트이엔씨 | System for reducing fine dust |
| FR3102682B1 (en) | 2019-11-03 | 2021-09-24 | Weber Jean Charles | Filtration device for polluted gases by absorption |
| CN111735150A (en) * | 2020-07-27 | 2020-10-02 | 王新 | an air purifier |
| DE102021114987A1 (en) | 2021-06-10 | 2022-12-15 | Topas Gmbh Technologieorientierte Partikel-, Analysen- Und Sensortechnik | Device for generating a conditioned aerosol |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE151261C (en) * | ||||
| CH368916A (en) * | 1959-05-28 | 1963-04-30 | Wera Apparatebau Ag | Air humidification system, in particular for ventilation and air conditioning systems |
| IL45916A (en) * | 1974-10-23 | 1976-11-30 | Rosenberg Peretz | Spray-nozzle |
| AU531724B2 (en) * | 1980-03-06 | 1983-09-01 | Masahiko Izumi | Microbe removing + air-conditioning apparatus |
| JPS5998714A (en) * | 1982-11-30 | 1984-06-07 | Masahiko Izumi | Preparation of gas suspending fine water droplet |
| JPS6058255A (en) * | 1983-09-09 | 1985-04-04 | Matsushita Electric Ind Co Ltd | Spray apparatus |
-
1985
- 1985-09-21 JP JP60207767A patent/JPS6268515A/en active Granted
-
1986
- 1986-09-05 DK DK426086A patent/DK426086A/en not_active Application Discontinuation
- 1986-09-05 SE SE8603728A patent/SE8603728L/en not_active Application Discontinuation
- 1986-09-09 IN IN723/MAS/86A patent/IN168582B/en unknown
- 1986-09-09 AU AU62505/86A patent/AU577203B2/en not_active Ceased
- 1986-09-10 CA CA000517874A patent/CA1265435A/en not_active Expired - Lifetime
- 1986-09-11 FR FR868612689A patent/FR2587628B1/en not_active Expired
- 1986-09-11 IT IT48442/86A patent/IT1196617B/en active
- 1986-09-15 NL NL8602323A patent/NL8602323A/en not_active Application Discontinuation
- 1986-09-17 KR KR1019860007837A patent/KR910005982B1/en not_active Expired
- 1986-09-17 GB GB8622410A patent/GB2180776B/en not_active Expired
- 1986-09-17 BR BR8604462A patent/BR8604462A/en unknown
- 1986-09-19 CH CH3764/86A patent/CH669834A5/fr not_active IP Right Cessation
- 1986-09-19 DE DE19863631926 patent/DE3631926A1/en not_active Withdrawn
- 1986-09-20 CN CN86106342.2A patent/CN1004860B/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| CH669834A5 (en) | 1989-04-14 |
| DK426086A (en) | 1987-03-22 |
| BR8604462A (en) | 1987-05-19 |
| IT1196617B (en) | 1988-11-16 |
| GB8622410D0 (en) | 1986-10-22 |
| KR870002866A (en) | 1987-04-13 |
| GB2180776A (en) | 1987-04-08 |
| SE8603728D0 (en) | 1986-09-05 |
| CN1004860B (en) | 1989-07-26 |
| NL8602323A (en) | 1987-04-16 |
| DE3631926A1 (en) | 1987-03-26 |
| FR2587628B1 (en) | 1989-06-23 |
| KR910005982B1 (en) | 1991-08-09 |
| AU577203B2 (en) | 1988-09-15 |
| IT8648442A1 (en) | 1988-03-11 |
| DK426086D0 (en) | 1986-09-05 |
| IN168582B (en) | 1991-05-04 |
| SE8603728L (en) | 1987-03-22 |
| CN86106342A (en) | 1987-04-08 |
| JPS6268515A (en) | 1987-03-28 |
| CA1265435A (en) | 1990-02-06 |
| IT8648442A0 (en) | 1986-09-11 |
| GB2180776B (en) | 1989-09-13 |
| AU6250586A (en) | 1987-03-26 |
| FR2587628A1 (en) | 1987-03-27 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |