JPS6138643A - Dust collector - Google Patents

Dust collector

Info

Publication number
JPS6138643A
JPS6138643A JP16114884A JP16114884A JPS6138643A JP S6138643 A JPS6138643 A JP S6138643A JP 16114884 A JP16114884 A JP 16114884A JP 16114884 A JP16114884 A JP 16114884A JP S6138643 A JPS6138643 A JP S6138643A
Authority
JP
Japan
Prior art keywords
gas
section
dust collecting
water vapor
dust
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP16114884A
Other languages
Japanese (ja)
Inventor
Isao Miyahara
宮原 勇郎
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP16114884A priority Critical patent/JPS6138643A/en
Publication of JPS6138643A publication Critical patent/JPS6138643A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To increase the dust collecting effect and to prolong the life of dust collecting part in a dust collector by providing the dust collecting part, the first moistening part of gas suction side, the second moistening part of gas discharge side and a blast part. CONSTITUTION:The gas contg. fine particles which is sent from a suction pipe 2 is electrified in an ionization part 309 and the water vapor of pure water fed from the first moistening part 301 is mixed with the gas and the joining of water molecule to the fine particles is quickly accelerated and the quantity of the fine particles caught by a dust collecting part 303 becomes remarkably much and the dust collecting effect is made high. The water vapor of pure water fed from the second moistening part 305 is mixed with the gas which has been passed through the dust collecting part and the gas is passed through a blower 307 and sent to a clean chamber 1 and diffused.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、気体中の塵、金属イオン等を除去する集塵装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a dust collector that removes dust, metal ions, etc. from gas.

(従来技術) 従来、電子工業1機械工業、化学工業等の分野において
は、室内の気体中の塵や金属イオン等の微粒子を除去す
る集塵装置が使用されている。
(Prior Art) Conventionally, in fields such as electronic industry, mechanical industry, and chemical industry, dust collectors have been used to remove fine particles such as dust and metal ions from indoor gases.

このため、従来は集塵装置としてフィルター(通常は粒
径0’、171mの微粒子の捕捉率99゜9995、%
のいわゆるHEPAフィルター)を用い、気体中の塵や
金属イオン(金属イオンは特にレーザー加工で金属を加
工する場合等に多量に発生する)等の除去は、気流を該
フィルターに通し、フィルター上に塵や金属イオンを捕
捉することによって行なっていた。
For this reason, in the past, filters were used as dust collectors (usually with a capture rate of 99°9995% for fine particles with particle diameters of 0' and 171 m).
A so-called HEPA filter) is used to remove dust and metal ions (metal ions are generated in large quantities especially when processing metal with laser processing) in the gas, by passing the air flow through the filter and placing it on the filter. This was done by trapping dust and metal ions.

(従来技術の問題点) しかしながら、近年は、気体中の微粒子の内、粒径0 
、1 pm以下のものの集塵装置による除去が要求され
、また、集塵装置を通過する微粒子の密度に対する制限
もきびしくなっており、上記のフィルター・による集塵
装置によっては、粒径O1lpm以下の微粒子は捕捉し
にくくなるばかりか、集塵装置を通過する微粒子の密度
の点でも近年の集塵装置に対する要求を満足できないも
のとなっている。
(Problems with conventional technology) However, in recent years, among fine particles in gas, particle size 0
, 1 pm or less is required to be removed by a dust collector, and restrictions on the density of fine particles passing through the dust collector are becoming stricter. Not only is it difficult to capture fine particles, but also the density of fine particles passing through the dust collector cannot satisfy recent demands for dust collectors.

また、従来のフィルターによる集塵装置はフィルターに
捕捉された微粒子はそのままフィルター上に残るため、
フィルターの使用時間が長くなればフィルターが目詰り
を起し、また一度フイルターで補%した微粒子が剥れて
再び飛散することもあり、これらによって、微粒子の捕
捉状態が悪化するばかりか、フィルターの寿命も短く、
また捕捉した微粒子を処理するためには該フィルターを
取換えなければならなかった。
In addition, with conventional filter-based dust collectors, fine particles captured by the filter remain on the filter.
If the filter is used for a long time, the filter will become clogged, and the particles that have been supplemented by the filter may peel off and be scattered again, which not only worsens the condition of capturing particles, but also causes the filter to become clogged. The lifespan is short,
In addition, the filter had to be replaced in order to dispose of the trapped particles.

(発明の目的) 本発明の目的は、微粒子の粒径が水の分子程度からO,
lpLm程度のものをも有効に除去出来る集塵装置を提
供することにある。
(Object of the invention) The object of the present invention is to reduce the particle size of fine particles from about the size of a water molecule to O,
It is an object of the present invention to provide a dust collector capable of effectively removing particles of about lpLm.

本発明の他の目的は、集塵装置を長時間使用しても微粒
子の捕捉状態が悪化せず、また、集塵装置の集塵部分の
寿命を極めて長く出来るとともに、捕捉した微粒子を容
易に排出出来る集塵装置を提供することにある。
Another object of the present invention is that even if the dust collector is used for a long time, the state of capturing fine particles does not deteriorate, and the life of the dust collecting part of the dust collector can be extremely extended, and the trapped fine particles can be easily removed. The purpose of the present invention is to provide a dust collector that can discharge dust.

本発明のさらに他の目的は、気体中から雑菌の除去も効
果的に行なえる集塵装置を提供することにある。
Still another object of the present invention is to provide a dust collector that can effectively remove germs from gas.

(発明の概要) 本発明は、気体中の水蒸気と結合した粒子を集塵除去す
る集塵部303と、該集塵部の気体吸入側に設けられ吸
入される気体中に水蒸気を供給する第一の加湿部301
と、該集塵部の気体排出側に設けられ集塵後の気体に水
蒸気を供給する第二の加湿部305と、該集塵部に気体
を循環させる送風部307とを有する集塵装置3を提供
するものであり、また、本発明は、気体中の水蒸気と結
合した粒子を集塵除去する集塵部303と、該集塵部の
気体吸入側に設けられ吸入される気体中に水蒸気を供給
する第一の加湿部301と、該第一の加湿部の気体吸入
側に設けられ気体中の粒子をイオン化するイオン化部3
09と、該集塵部の気体排出側に設けられ集塵後の気体
に水蒸気を供給する第二の加湿部305と、該集塵部に
気体を循環させる送風部307とを有する集塵装置3を
提供するものであり、さらに、本発明は、気体中の水蒸
気と結合した粒子を集塵除去する第一の集塵部303と
、該第一の集塵部の気体吸入側に設けられ吸入される気
体中に水蒸気を供給する第一の加湿部301と、該第一
の加湿部の気体吸入側に設けられ気体中の粒子をイオン
化するイオン化部309と、該第一の集塵部の気体排出
側に設けられ集塵後の気体に水蒸気を供給する第二の加
湿部305と、イオン化部の気体吸入側に設けられ気体
中の水蒸気と結合した粒子を集塵除去する第二の集塵部
313と、該第二の集塵部の気体吸入側に設けられ吸入
される気体中に水蒸気を供給する第三の加湿部311と
、第一及び第二の集塵部に気体を循環させる送風部30
7とを有する集塵装置3を提供するものである。
(Summary of the Invention) The present invention includes a dust collection section 303 that collects and removes particles combined with water vapor in a gas, and a dust collection section 303 that is provided on the gas suction side of the dust collection section and supplies water vapor into the gas to be inhaled. No. 1 humidifying section 301
, a second humidifying section 305 that is provided on the gas discharge side of the dust collecting section and supplies water vapor to the gas after dust collection, and a blowing section 307 that circulates the gas to the dust collecting section. The present invention also provides a dust collecting section 303 that collects and removes particles combined with water vapor in the gas, and a dust collecting section 303 that is provided on the gas suction side of the dust collecting section to remove water vapor from the inhaled gas. a first humidifying section 301 that supplies a gas, and an ionizing section 3 that is provided on the gas suction side of the first humidifying section and ionizes particles in the gas.
09, a second humidifying section 305 that is provided on the gas discharge side of the dust collecting section and supplies water vapor to the gas after dust collection, and a blowing section 307 that circulates the gas to the dust collecting section. Further, the present invention provides a first dust collecting section 303 that collects and removes particles combined with water vapor in the gas, and a first dust collecting section 303 that is provided on the gas suction side of the first dust collecting section. A first humidifying section 301 that supplies water vapor into the gas to be inhaled, an ionizing section 309 that is provided on the gas suction side of the first humidifying section and ionizes particles in the gas, and a first dust collecting section. A second humidifying section 305 is provided on the gas discharge side of the ionization section and supplies water vapor to the gas after dust collection; A dust collecting section 313, a third humidifying section 311 that is provided on the gas suction side of the second dust collecting section and supplies water vapor into the inhaled gas, and a third humidifying section 311 that supplies water vapor to the first and second dust collecting sections. Air blowing unit 30 for circulation
7 is provided.

(実施例) 以下、本発明について詳細に説明する。(Example) The present invention will be explained in detail below.

第1図は本発明の一実施例を示す概略図で、1は塵等の
除去の必要なりリーンルーム、2はクリーンルーム1の
気体を本発明に係る集塵装置3に送風する吸入パイプ、
4は該集塵装置3からの集塵後の気体をクリーンルーム
1内に送風する排気パイプである。
FIG. 1 is a schematic diagram showing an embodiment of the present invention, in which 1 is a lean room where it is necessary to remove dust, etc., 2 is a suction pipe that blows gas from the clean room 1 to a dust collector 3 according to the present invention;
Reference numeral 4 denotes an exhaust pipe for blowing the gas after dust collection from the dust collector 3 into the clean room 1.

301は、吸入パイプ2内に水蒸気(H20ガス)を送
風し、クリーンルーム1からの気体と該水蒸気を混合す
る第一の加湿部、303は、気体中の塵等を集める集塵
部、305は集塵後の気体中に水蒸気を混合する第二の
加湿部、’−307は気体の循環を行なう送風部である
301 is a first humidifying section that blows water vapor (H20 gas) into the suction pipe 2 and mixes the water vapor with gas from the clean room 1; 303 is a dust collection section that collects dust, etc. in the gas; 305 is a The second humidifying section '-307 that mixes water vapor into the gas after dust collection is a blowing section that circulates the gas.

以下、集塵装置3内の各構成部分を詳細に説明する。Each component within the dust collector 3 will be described in detail below.

第一の加湿部301及び第二の加湿部305は、純水の
水蒸気を発生させ該水蒸気を気体中に混合するものであ
るが、この水蒸気の発生装置には、種々の装置が考えら
れ、例えば水槽中に電気ヒータを挿入する装置、ボイラ
ーよりの乾燥加熱水蒸気を導く装置、超音波振動により
水蒸気を発生させる装置、赤外線水蒸気発生装置等があ
る。
The first humidifying section 301 and the second humidifying section 305 generate pure water vapor and mix the vapor into gas, and various devices can be considered as the steam generating device. For example, there are devices that insert an electric heater into a water tank, devices that introduce dry heated steam from a boiler, devices that generate steam using ultrasonic vibrations, and infrared steam generators.

集塵部303を構成する装置としては、気体中の水蒸気
を気体から分離する装置であればよく、例えば、公知の
冷却器(バッフル式冷却器、フィンコイル式冷却器等)
や、冷却された純水、塩水等のシャワー装置や、気体と
液体を分離するエリミネータ等や、これらの装置を適当
に組合せたものを用いる。なお、冷却器やシャワー装置
等のように気体自体を冷却する装置を用いた場合は、第
2図に示すように、集塵部303へ後に、この冷却され
た気体を加熱するヒータ等からなる公知の加熱手段から
なる加熱部304を設けることが好ましい。
The device constituting the dust collecting section 303 may be any device that separates water vapor in gas from gas, such as a known cooler (baffle type cooler, fin coil type cooler, etc.).
A shower device using cooled pure water, salt water, etc., an eliminator that separates gas and liquid, or an appropriate combination of these devices are used. Note that when a device that cools the gas itself, such as a cooler or a shower device, is used, as shown in FIG. It is preferable to provide a heating section 304 made of known heating means.

送風部307は、電動式ファン等の、気体を送風する公
知の種々の装置で構成される。
The blower section 307 is configured with various known devices for blowing gas, such as an electric fan.

次に本発明の詳細な説明する。Next, the present invention will be explained in detail.

集塵部303を通過した気体には第二の加湿部305に
より純水の水蒸気が混合され、この水蒸気を含む気体は
送風部307を通過してクリーンルーム1内に送られ拡
散される。ここでH2Oの分子は水素原子2個と酸素分
子1個により構成されているが、その構造は第3図に示
すように分極している。H20分子はこの両極間の距離
が他の分子に比べ非常に大きく、液体にあってはH20
20分子第4図に示すように水素結合力で強く引き合う
。このようなH20分子が空間に拡散されれば、該H2
0分子は、第5図(a)、(b)。
The gas that has passed through the dust collecting section 303 is mixed with pure water vapor by the second humidifying section 305, and the gas containing this water vapor is sent into the clean room 1 through the blowing section 307 and diffused. Here, the molecule of H2O is composed of two hydrogen atoms and one oxygen molecule, and its structure is polarized as shown in FIG. The distance between the two poles of H20 molecules is very large compared to other molecules, and in liquids, H20
As shown in Figure 4, 20 molecules are strongly attracted to each other by hydrogen bonding forces. If such H20 molecules are diffused into space, the H20 molecules
0 molecules are shown in Figures 5(a) and (b).

(C)に示すように、気体中の帯電又は分極している微
粒子7に対し強力なり−ロンカで結びっ〈。第5図(a
)にあっては、十に帯電した微粒子7の回りにH20分
子が結合し、全体としてひとまわり大きな十の微粒子と
なる状態を示す。第5図(b)にあっては、−に帯電し
た微粒子7の回りにH20分子が結合し、全体としてひ
とまわり大きな−の微粒子となる状態を示す。第5図(
C)にあっては、十と−に分極した微粒子7の回りにH
20分子が結合し、全体としてひとまわり大きな分極微
粒子となる状態を示す。そしてH2o分子が結合した微
粒子はその表面積が増大するため増々H20分子の結合
を促すようになる。
As shown in (C), it is strong against charged or polarized fine particles 7 in the gas and is connected with a ronca. Figure 5 (a
) shows a state in which H20 molecules bond around the ten-charged fine particles 7, forming ten-sized fine particles that are one size larger as a whole. FIG. 5(b) shows a state in which H20 molecules are bonded around the negatively charged fine particles 7, resulting in a slightly larger negative fine particle as a whole. Figure 5 (
In C), H is formed around the fine particle 7 polarized to
This shows a state in which 20 molecules combine to form a polarized fine particle that is one size larger as a whole. Since the surface area of the fine particles to which H2o molecules are bound increases, the binding of H20 molecules becomes more and more likely to occur.

つまり、クリーンルームl内の気体中を浮遊している微
粒子が十又は−に帯電又は分極していれば、これらの微
粒子を核としてH20分子が結合し、又、このようにH
20分子が結合した微粒子も相互に結合し、大きな粒子
を形成してゆく(これは大気中の水蒸気が微粒子を核と
して雲や雨を形・成する過程と同一である)。
In other words, if the fine particles floating in the gas in the clean room l are charged or polarized, H20 molecules will combine with these fine particles as nuclei, and in this way H20 molecules will combine with these fine particles as nuclei.
Fine particles made up of 20 molecules also combine with each other to form larger particles (this is the same process in which water vapor in the atmosphere forms clouds and rain using fine particles as cores).

ただし、クリーンルーム1内に第二の加湿部305によ
って純水の水蒸気を送り込んだ状態では微粒子とH20
分子の結合したものは、それほど成長せず、また、中に
は全<H2Oの結合しない微粒子も存在するものと考え
られる。
However, when pure water vapor is sent into the clean room 1 by the second humidifying unit 305, fine particles and H20
It is thought that those with bound molecules do not grow as much, and that there are also fine particles in which all <H2O is not bound.

なお、クリーンルーム1内での作業上又は集塵効果上、
水蒸気が不純物を含むことは好ましくなく、また、第二
の加湿部305から発生させる水蒸気は、そのH20分
子数が増加すれば、クリーンルームl内で、H20分子
と微粒子とが結合する頻度が増えるが、同じ湿度でH2
0分子数を多くするためにはH20分子がなるべく単独
の状態の水蒸気、即ち熱エネルギーの高い完全なガス状
態の水蒸気であ・ることが好ましい。このため第二の加
湿部305は、゛上述の種々の水蒸気発生装置の内、近
赤外線領域の電磁波を水槽内の氷表面に照射して水中内
沸騰を起さず表面より短時間で蒸発させ、はぼ100%
近い割合の純水乾燥加熱水蒸気を得ることが出来、上記
の他の種々の水蒸気発生装置に比べH20以外の種々の
物質、気体が水蒸気とともに飛び出すことが少なく、ま
た、発生される水蒸気は飽和水蒸気ではないので気体と
混合後にその凝縮が生じにくく完全なガス状態を保てる
赤外線水蒸気発生装置が、最も好適である。
In addition, due to work in clean room 1 or dust collection efficiency,
It is undesirable for the water vapor to contain impurities, and as the number of H20 molecules in the water vapor generated from the second humidifying section 305 increases, the frequency of bonding between H20 molecules and fine particles in the clean room 1 increases. , H2 at the same humidity
In order to increase the number of zero molecules, it is preferable that the H20 molecules be water vapor in a single state as much as possible, that is, water vapor in a complete gas state with high thermal energy. For this reason, the second humidifying unit 305 is one of the above-mentioned various water vapor generating devices that irradiates electromagnetic waves in the near-infrared region to the ice surface in the water tank to evaporate water from the surface in a short time without causing boiling in the water. , Habo 100%
It is possible to obtain pure water dry heating steam with a similar ratio, and compared to the other various steam generators mentioned above, various substances and gases other than H20 are less likely to be ejected together with the steam, and the steam generated is saturated steam. Therefore, an infrared steam generator is most suitable because it is difficult to condense after mixing with gas and can maintain a perfect gas state.

次に、クリーンルームl内でH20分子と結合した微粒
子やH20分子と結合しない微粒子を含む気体は、吸入
パイプ2から集塵装置3内に導入される。導入された気
体には第一の加湿部301(水蒸気発生装置としては上
記の第二の加湿部305の説明と同様に赤外線水蒸気発
生装置が最も好ましい)から発生される純水の水蒸気が
さらに混合され、クリーンルーム1内ではH20分子と
結合しなかった微粒子の多くがH20分子と結合し、ま
た、すてにH20分子が結合した微粒子にもざらにH2
0分子が結合し、その粒径を拡大し、これらの微粒子や
H20分子を含む気体はさらに集塵部303へと送られ
る。
Next, the gas containing fine particles bound to H20 molecules and fine particles not bound to H20 molecules in the clean room 1 is introduced into the dust collector 3 from the suction pipe 2. The introduced gas is further mixed with pure water vapor generated from the first humidifying section 301 (as the steam generating device, an infrared steam generator is most preferable as in the explanation of the second humidifying section 305 above). In clean room 1, many of the particles that did not bond with H20 molecules bonded with H20 molecules, and some of the particles that had H20 molecules bonded with them were also exposed to H2.
The H20 molecules combine to expand their particle size, and the gas containing these fine particles and H20 molecules is further sent to the dust collecting section 303.

集塵部303へ送られた気体は、ここで微粒子やH20
分子と分離させられるのであるが、以下この作用を説明
する。
The gas sent to the dust collection section 303 collects fine particles and H20 there.
This effect is explained below.

即ち、集塵部303を構成する冷却器内又はシャワー装
置内へ送られた気体は、その気体の露点以下の温度とさ
れる。そしてこの気体は、粒径を拡大した微粒子(H2
0分子・と結合していない微粒子を含む)を核として凝
縮を起し、これが水滴となって冷却器の吸熱板表面又は
純水や塩水表面に付着する。そして、微粒子を含む水滴
は冷却装置のドレンやシャワー装置のドレンを介して排
出除去される。これによって、気体中の塵や金属イオン
等の微粒子は取り除かれる。ここで第2図     ・
に示すように集塵部303の後に加熱部304を設けた
場合は、気体中の微粒子が取り除かれた後の冷却された
気体を加熱部304によって急速に加熱でき、該気体は
湿度が低くなり、その後に第二の加湿部305によって
供給される純水の水蒸気を受は入れる能力が増大する。
That is, the temperature of the gas sent into the cooler or shower device that constitutes the dust collecting section 303 is lower than the dew point of the gas. Then, this gas contains fine particles (H2
Condensation occurs with the particles (including fine particles not bonded to molecules) as the core, which becomes water droplets and adheres to the surface of the heat absorption plate of the cooler or the surface of pure water or salt water. The water droplets containing fine particles are then discharged and removed through the drain of the cooling device or the drain of the shower device. This removes fine particles such as dust and metal ions in the gas. Here, Figure 2 ・
When the heating section 304 is provided after the dust collection section 303 as shown in Fig. 3, the cooling section 304 can rapidly heat the cooled gas after fine particles in the gas have been removed, and the humidity of the gas becomes low. Then, the ability to receive the pure water vapor supplied by the second humidifying section 305 increases.

なお、集塵部303を気体と液体を分離するエリミネー
タで構成した場合もエリミネータ表面に付着した水滴は
ドレンを通して外部に排出除去できる。
Note that even when the dust collecting section 303 is configured with an eliminator that separates gas and liquid, water droplets attached to the surface of the eliminator can be discharged and removed to the outside through the drain.

また、上記の冷却器とシャワー装置とエリミネータとを
種々組合せて集塵部303を構成した場合は、集塵部3
03の集塵効果はさらに増大する。
In addition, when the dust collecting section 303 is configured by various combinations of the above-mentioned cooler, shower device, and eliminator, the dust collecting section 303
The dust collection effect of 03 is further increased.

なお、送風部307は本実施例においては排気パイプ4
側に設けられているが、該送風部307は集塵装置の他
の部分に設けてもよいことは言うまでもない。
Note that the blower section 307 is the exhaust pipe 4 in this embodiment.
Although it is provided on the side, it goes without saying that the air blowing section 307 may be provided on other parts of the dust collector.

また、この集塵装置は第1図に示す集塵装置3を複数併
設してもよく、このように構成すれば集塵効果はさらに
増大する。
Moreover, this dust collector may be provided with a plurality of dust collectors 3 shown in FIG. 1, and if configured in this way, the dust collection effect will be further increased.

第6図は上記実施例で説明した発明を改良した集塵装置
を示す概略図で、第1図に示す集塵装置よりさらに集塵
効果を増大させたものである。
FIG. 6 is a schematic diagram showing a dust collector improved from the invention described in the above embodiment, and has a greater dust collection effect than the dust collector shown in FIG.

同図中第1図と同一部分には同一符号を付し、その詳細
な説明は省略する。
In the figure, the same parts as in FIG. 1 are denoted by the same reference numerals, and detailed explanation thereof will be omitted.

同図中1はクリーンルーム、2は吸入パイプ、3は集塵
装置、4は排気パイプ、301は第一の加湿部、303
は集塵部、305は第二の加湿部、307は送風部であ
り、第1図の集塵装置と同じである。309はイオン化
部であり、該イオン化BB309を通過する気1体中の
微粒子はイオン化される。第7図はこのイオン化部30
9の一実施例を詳珂に説明する図である。同図中8はた
とえばタングステンの線で構成された放電極で、高電圧
が印加されている(例えば9KV)。9はアース極で、
放電極8との間で放電を起こす。そしてこの放電極8.
アース極9間を気体が通過する時(矢印A方向)に、−
又は中性の微粒子自体は十に帯電することとなる(すで
に十に帯電している微粒子もその帯電の量が増す)。
In the figure, 1 is a clean room, 2 is an intake pipe, 3 is a dust collector, 4 is an exhaust pipe, 301 is a first humidifying section, 303
305 is a dust collecting section, 305 is a second humidifying section, and 307 is a blowing section, which are the same as the dust collecting device shown in FIG. 309 is an ionization section, and fine particles in the gas passing through the ionization BB 309 are ionized. FIG. 7 shows this ionization section 30.
FIG. 9 is a diagram illustrating an embodiment of No. 9 in detail. In the figure, reference numeral 8 denotes a discharge electrode made of, for example, a tungsten wire, to which a high voltage (for example, 9 KV) is applied. 9 is the earth pole,
A discharge is caused between the discharge electrode 8 and the discharge electrode 8. And this discharge electrode 8.
When gas passes between the earth electrodes 9 (in the direction of arrow A), -
Alternatively, the neutral fine particles themselves become charged to 10 (the amount of charge of fine particles that are already 10 charged also increases).

すなわち、吸入パイプ2から送られてくるH20分子と
結合した微粒子やいまだH20分子と結合していない微
粒子は十に帯電され、このような微粒子を含む気体に第
一の加湿部301から純水の水蒸気が混合されると微粒
子へのH20分子の結合が急速に促され、その粒径を増
々増大して。
That is, fine particles that have bound to H20 molecules sent from the suction pipe 2 and fine particles that have not yet bound to H20 molecules are highly charged, and pure water is added to the gas containing such fine particles from the first humidifying section 301. When water vapor is mixed, the binding of H20 molecules to the fine particles is rapidly promoted, increasing the particle size.

集塵部303で捕捉される微粒子の量が非常に多〈なり
、集塵効果が増大する。
The amount of fine particles captured by the dust collection section 303 becomes extremely large, and the dust collection effect increases.

なお、イオン化部の放電極8には−の高電圧を印加して
もよいことは言うまでもなく、この場合は気体中の微粒
子は−に帯電される。
It goes without saying that a negative high voltage may be applied to the discharge electrode 8 of the ionization section, and in this case, the fine particles in the gas will be negatively charged.

第8図は、上記の第6図に示す発明をさらに改良した集
塵装置を示す概略図である。
FIG. 8 is a schematic diagram showing a dust collector which is a further improvement of the invention shown in FIG. 6 above.

同図中第6図と同一部分には同一符号を付し、その詳細
な説明は省略する。
In the figure, the same parts as in FIG. 6 are designated by the same reference numerals, and detailed explanation thereof will be omitted.

同図中1はクリーンルーム、2は吸入パイプ、3は集塵
装置、4は排気パイプであり、301は第一の加湿部、
303は集塵部(第一の集塵部)、305は第二の加湿
部、307は送風部、309はイオン化部であり、第6
図の集塵装置と同じである。311は第三の加湿部であ
り、その水蒸気発生装置としては第一の加湿部301.
第二の加湿部305と同様に赤外線水蒸気発生装置が最
も好ましい。313は第二の集塵部であり、第一の集塵
部303と同様に冷却器、シャワー装置又はエリミネー
タ等や、これらの装置を適当に組合せたものを用いる。
In the figure, 1 is a clean room, 2 is an intake pipe, 3 is a dust collector, 4 is an exhaust pipe, 301 is a first humidifying section,
303 is a dust collection part (first dust collection part), 305 is a second humidification part, 307 is a ventilation part, 309 is an ionization part, and the sixth
This is the same as the dust collector shown in the figure. 311 is a third humidifying section, and its water vapor generating device is the first humidifying section 301.
Like the second humidifying section 305, an infrared steam generator is most preferable. A second dust collecting section 313 uses a cooler, a shower device, an eliminator, etc., or a suitable combination of these devices, like the first dust collecting section 303.

第6図に示す集塵装置の気体吸入側に新たに第三の加湿
部311と第二の集塵部313を設けたので、集塵効果
はさらに増すこととなる。
Since a third humidifying section 311 and a second dust collecting section 313 are newly provided on the gas suction side of the dust collector shown in FIG. 6, the dust collecting effect is further increased.

なお、以上の各実施例においては、集塵装置をクリーン
ルームに用いた場合を示したが、本発明は、これに限ら
れず1通常の室内の集塵装置や、また、外気を室内に取
り入る場合の集塵装置として使用する場合等、他の種々
の集塵を必要とする場合の集塵装置として使用できるも
のである。
In each of the above embodiments, the case where the dust collector is used in a clean room is shown, but the present invention is not limited to this, and can be applied to a normal indoor dust collector or when outside air is taken into the room. The present invention can be used as a dust collector in various other cases where dust collection is required, such as when used as a dust collector.

また、本発明に係る集塵装置は、空調機能を有するので
一般の空調装置内に組み込むことは有益である。
Further, since the dust collector according to the present invention has an air conditioning function, it is advantageous to incorporate it into a general air conditioner.

(発明の効果) 以上詳細に説明したように、本発明によれば、微粒子の
粒径が水の分子程度(はぼQ、0004gm)から0.
1pm程度のものをもH20分子によって拡大し有効に
除去出来るし、これによって気体中からの雑菌の除去も
効果的に行なえる。
(Effects of the Invention) As described above in detail, according to the present invention, the particle size of the fine particles ranges from about the size of a water molecule (Habo Q, 0004 gm) to about 0.5 gm.
Even particles with a particle size of about 1 pm can be expanded and effectively removed by H20 molecules, and thereby bacteria can also be effectively removed from the gas.

また、本発明によれば、従来のフィルタによる集塵装置
に比較し、集塵装置を長時間使用してもその集塵部に集
塵された微粒子は液体となった水といっしょに容易に排
出でき、微粒子の捕捉状態が悪化せず、また、集塵装置
の集塵部の寿命を極めて長く出来る。
Furthermore, according to the present invention, compared to a conventional dust collector using a filter, even if the dust collector is used for a long time, the fine particles collected in the dust collector are easily collected together with liquid water. It can be discharged without deteriorating the state of capturing fine particles, and the life of the dust collection part of the dust collection device can be extremely extended.

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

第1図は本発明に係る集塵装置を示す概略図、第2図は
第1図に示す集塵部303の後に加熱部304を設けた
構成の一実施例を示す図、第3図は水分子の形状を示す
図、第4図は水分子間の引力の状態を示す図、第5図(
a)、(b)、(c)は微粒子と水分子との結合状態を
示す図、第6図は第1図で説明した発明を改良した集塵
装置を示す概略図、第7図は第6図に示すイオン化部3
09の一実施例を詳細に説明する図、第8図は、上記の
第6図に示す発明をさらに改良した集塵装置を示す概略
図である。 1−・クリーンルーム 2−・吸入パイプ3・φ集塵装
置 301−・第一の加湿部303・・集塵部(第一の
集塵部) 305・・第二の加湿部 307・・送風部4・・排気
パイプ 304・・加熱部 8・・放電極 9φ・アース極 309・・イオン化部311・・第三
の加湿部 313・・第二の集塵部
FIG. 1 is a schematic diagram showing a dust collector according to the present invention, FIG. 2 is a diagram showing an example of a configuration in which a heating section 304 is provided after the dust collecting section 303 shown in FIG. 1, and FIG. Figure 4 shows the shape of water molecules, Figure 4 shows the state of attraction between water molecules, Figure 5 (
a), (b), and (c) are diagrams showing the bonding state of fine particles and water molecules, Figure 6 is a schematic diagram showing a dust collector improved from the invention explained in Figure 1, and Figure 7 is a diagram showing the state of bonding between fine particles and water molecules. Ionization section 3 shown in Figure 6
FIG. 8, which is a diagram illustrating one embodiment of No. 09 in detail, is a schematic diagram showing a dust collector that is a further improvement of the invention shown in FIG. 6 above. 1-.Clean room 2-.Suction pipe 3.φ dust collector 301-.First humidifying section 303..Dust collecting section (first dust collecting section) 305..Second humidifying section 307..Blower section 4...Exhaust pipe 304...Heating section 8...Discharge electrode 9φ/earth electrode 309...Ionization section 311...Third humidifying section 313...Second dust collecting section

Claims (3)

【特許請求の範囲】[Claims] (1)気体中の水蒸気と結合した粒子を集塵除去する集
塵部と、該集塵部の気体吸入側に設けられ吸入される気
体中に水蒸気を供給する第一の加湿部と、該集塵部の気
体排出側に設けられ集塵後の気体に水蒸気を供給する第
二の加湿部と、該集塵部に気体を循環させる送風部とを
有する集塵装置。
(1) a dust collecting section that collects and removes particles combined with water vapor in the gas; a first humidifying section that is provided on the gas suction side of the dust collecting section and supplies water vapor into the gas to be inhaled; A dust collector having a second humidifying part provided on the gas discharge side of the dust collecting part and supplying water vapor to the gas after dust collection, and a blowing part circulating the gas in the dust collecting part.
(2)気体中の水蒸気と結合した粒子を集塵除去する集
塵部と、該集塵部の気体吸入側に設けられ吸入される気
体中に水蒸気を供給する第一の加湿部と、該第一の加湿
部の気体吸入側に設けられ気体中の粒子をイオン化する
イオン化部と、該集塵部の気体排出側に設けられ集塵後
の気体に水蒸気を供給する第二の加湿部と、該集塵部に
気体を循環させる送風部とを有する集塵装置。
(2) a dust collecting section that collects and removes particles combined with water vapor in the gas; a first humidifying section that is provided on the gas suction side of the dust collecting section and supplies water vapor into the inhaled gas; an ionization section that is provided on the gas suction side of the first humidification section and ionizes particles in the gas; a second humidification section that is provided on the gas discharge side of the dust collection section that supplies water vapor to the gas after dust collection; , and a blowing section that circulates gas through the dust collecting section.
(3)気体中の水蒸気と結合した粒子を集塵除去する第
一の集塵部と、該第一の集塵部の気体吸入側に設けられ
吸入される気体中に水蒸気を供給する第一の加湿部と、
該第一の加湿部の気体吸入側に設けられ気体中の粒子を
イオン化するイオン化部と、該第一の集塵部の気体排出
側に設けられ集塵後の気体に水蒸気を供給する第二の加
湿部と、イオン化部の気体吸入側に設けられ気体中の水
蒸気と結合した粒子を集塵除去する第二の集塵部と、該
第二の集塵部の気体吸入側に設けられ吸入される気体中
に水蒸気を供給する第三の加湿部と、第一及び第二の集
塵部に気体を循環させる送風部とを有する集塵装置。
(3) A first dust collecting section that collects and removes particles combined with water vapor in the gas, and a first dust collecting section that is provided on the gas suction side of the first dust collecting section and supplies water vapor into the inhaled gas. a humidifying section,
an ionization section that is provided on the gas suction side of the first humidifying section and ionizes particles in the gas; and a second ionization section that is provided on the gas discharge side of the first dust collection section that supplies water vapor to the gas after dust collection. a second dust collecting part provided on the gas suction side of the ionization part to collect and remove particles combined with water vapor in the gas; A dust collector having a third humidifying section that supplies water vapor into the gas to be collected, and a blowing section that circulates the gas to the first and second dust collecting sections.
JP16114884A 1984-07-31 1984-07-31 Dust collector Pending JPS6138643A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16114884A JPS6138643A (en) 1984-07-31 1984-07-31 Dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16114884A JPS6138643A (en) 1984-07-31 1984-07-31 Dust collector

Publications (1)

Publication Number Publication Date
JPS6138643A true JPS6138643A (en) 1986-02-24

Family

ID=15729504

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16114884A Pending JPS6138643A (en) 1984-07-31 1984-07-31 Dust collector

Country Status (1)

Country Link
JP (1) JPS6138643A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62197441A (en) * 1986-02-24 1987-09-01 Takiron Co Ltd Chlorine-containing resin molding
CN110624340A (en) * 2019-09-18 2019-12-31 东南大学 Dust removal pretreatment device and method based on water vapor charge phase change

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62197441A (en) * 1986-02-24 1987-09-01 Takiron Co Ltd Chlorine-containing resin molding
CN110624340A (en) * 2019-09-18 2019-12-31 东南大学 Dust removal pretreatment device and method based on water vapor charge phase change

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