JP2006255662A - Air cleaner - Google Patents

Air cleaner Download PDF

Info

Publication number
JP2006255662A
JP2006255662A JP2005080265A JP2005080265A JP2006255662A JP 2006255662 A JP2006255662 A JP 2006255662A JP 2005080265 A JP2005080265 A JP 2005080265A JP 2005080265 A JP2005080265 A JP 2005080265A JP 2006255662 A JP2006255662 A JP 2006255662A
Authority
JP
Japan
Prior art keywords
counter electrode
air
electrode
discharge
treatment liquid
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
JP2005080265A
Other languages
Japanese (ja)
Inventor
Sadahiro Ogata
禎浩 緒方
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.)
Ricoh Elemex Corp
Original Assignee
Ricoh Elemex Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ricoh Elemex Corp filed Critical Ricoh Elemex Corp
Priority to JP2005080265A priority Critical patent/JP2006255662A/en
Publication of JP2006255662A publication Critical patent/JP2006255662A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Electrostatic Separation (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an air cleaner capable of making wetting property of a counter electrode uniform and reducing an amount of a treating liquid used. <P>SOLUTION: The air cleaner is provided with a discharge electrode arranged on a circulation route of air; and the counter electrode for capturing a component to be treated contained in air. Further, the air cleaner is provided with a treating liquid feeding means for feeding the treating liquid for absorbing the component to be treated to the counter electrode; and a treating liquid uniformizing means to make the treating liquid not to deviate by moving the counter electrode. Thereby, even if an amount of treating liquid used is small, the wetting property of the counter electrode can be made uniform. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、空気清浄機に関するものである。   The present invention relates to an air cleaner.

従来から、放電極と対向電極を備え、これらの間に電圧を印加して放電させるとともに、その放電によって空気中の粉塵などを帯電させて、対向電極に付着させる集塵装置が知られている。集塵装置には乾式集塵装置と湿式集塵装置がある。乾式集塵装置は、対向電極を打撃して振動させることで、対向電極の表面に付着した粉塵等を落下させるものであり、湿式集塵装置は、対向電極の表面に水等の流体を供給して液膜を形成して流下させ、この液膜によって粉塵等を除去するものである。   2. Description of the Related Art Conventionally, there is known a dust collector that includes a discharge electrode and a counter electrode, applies a voltage between them to discharge, and charges the dust in the air by the discharge to adhere to the counter electrode. . The dust collector includes a dry dust collector and a wet dust collector. The dry dust collector is designed to drop the dust attached to the surface of the counter electrode by striking and vibrating the counter electrode. The wet dust collector supplies a fluid such as water to the surface of the counter electrode. Then, a liquid film is formed and allowed to flow down, and dust and the like are removed by this liquid film.

湿式集塵装置としては例えば下記特許文献1および2が開示されている。特許文献1には、対向電極を金網状にするとともに水流膜を形成し、この水流膜に帯電した粒子成分を捕集させる方法が開示されており、特許文献2には、透水性被覆材を利用して筒状に形成し、その筒状体の内部に導電性を有する流体を充填した対向電極が開示されている。水流膜が形成された金網や、透水性被覆材を対向電極として利用することで、粉塵などを効果的に除去できる。
特許第3187205号公報 特許第2686881号公報
For example, Patent Documents 1 and 2 below are disclosed as wet dust collectors. Patent Document 1 discloses a method in which a counter electrode is formed into a wire mesh and a water film is formed, and charged particle components are collected in the water film. Patent Document 2 discloses a water-permeable coating material. There is disclosed a counter electrode that is formed into a cylindrical shape by use and is filled with a fluid having conductivity inside the cylindrical body. Dust and the like can be effectively removed by using a wire mesh formed with a water flow film or a water-permeable coating material as a counter electrode.
Japanese Patent No. 3187205 Japanese Patent No. 2,686,881

一方、従来の装置では、例えば図6に示すように、2枚の対向電極103の間に線状の放電極102を配置し、対向電極103と放電極102と間に電圧を印加することにより、放電を発生させている。空気は図6に示す装置の上方から下方へ流通し、放電領域Pを通過する。この時に、空気に含まれる粉塵やガス状成分等の被処理成分が放電領域Pにより帯電して、対向電極103に付着する。そして、対向電極103の内部または表面には水流膜が形成されて、付着した粉塵等を除去する。   On the other hand, in a conventional apparatus, for example, as shown in FIG. 6, a linear discharge electrode 102 is disposed between two counter electrodes 103 and a voltage is applied between the counter electrode 103 and the discharge electrode 102. The discharge is generated. The air flows from the upper side to the lower side of the apparatus shown in FIG. At this time, components to be treated such as dust and gaseous components contained in the air are charged by the discharge region P and adhere to the counter electrode 103. A water flow film is formed inside or on the surface of the counter electrode 103 to remove the adhering dust and the like.

ところが、対向電極103に水(処理液)を供給すると、水流膜が偏ってしまい、対向電極103の濡れ性が不均一になるという問題がある。濡れ性が不均一であると、空気と水の接触面積が小さくなり、その結果、被処理成分の除去効率が悪くなる。   However, when water (treatment liquid) is supplied to the counter electrode 103, the water flow film is biased and there is a problem that the wettability of the counter electrode 103 becomes non-uniform. If the wettability is not uniform, the contact area of air and water becomes small, and as a result, the removal efficiency of the component to be treated is deteriorated.

また、濡れ性を均一にするために処理液の供給量を増やすと、コストアップになったり、過度な液量により放電極と対向電極の間で短絡を引き起こしたりする問題が発生する。そのため、対向電極の濡れ性を均一にでき、かつ液量を少量化できる空気清浄機が望まれてきた。   Further, if the supply amount of the treatment liquid is increased in order to make the wettability uniform, there arises a problem that the cost increases or a short circuit is caused between the discharge electrode and the counter electrode due to an excessive liquid amount. Therefore, an air cleaner that can make the wettability of the counter electrode uniform and reduce the amount of liquid has been desired.

本発明は、上述のような事情を背景になされたもので、特に、対向電極の濡れ性を均一にでき、使用する処理液の量を少量化できる空気清浄機を提供することを課題とする。   The present invention has been made in the background as described above. In particular, it is an object of the present invention to provide an air purifier that can make the wettability of the counter electrode uniform and can reduce the amount of processing liquid to be used. .

課題を解決するための手段および発明の効果Means for Solving the Problems and Effects of the Invention

上記課題を解決するために本第1発明は、
空気の流通経路上に配置された放電極と、
空気中に含まれる被処理成分を捕集する対向電極と、
被処理成分を吸収する処理液を対向電極に供給する処理液供給手段と、
対向電極を動かすことにより、処理液が偏らないようにする処理液均一化手段と、
を備えることを主要な特徴とする。
In order to solve the above problems, the first invention
A discharge electrode disposed on the air flow path;
A counter electrode for collecting the component to be treated contained in the air;
A processing liquid supply means for supplying a processing liquid that absorbs the component to be processed to the counter electrode;
A processing liquid homogenizing means for preventing the processing liquid from being biased by moving the counter electrode;
The main feature is to have

上記第1発明によると、対向電極を動かすことにより、対向電極が処理液(例えば水)によって満遍なく濡れるようになる。その結果、空気と処理液の接触面積が増え、空気中に含まれる粉塵やガス状成分(例えばアンモニアや酢酸、硫化水素)を効率良く吸収することができる。また、使用する処理液の量が少なくても、濡れ性が均一になる。   According to the first aspect of the present invention, by moving the counter electrode, the counter electrode is uniformly wetted by the processing liquid (for example, water). As a result, the contact area between the air and the treatment liquid is increased, and dust and gaseous components (for example, ammonia, acetic acid, hydrogen sulfide) contained in the air can be efficiently absorbed. Moreover, even if the amount of the treatment liquid to be used is small, the wettability becomes uniform.

また、本第2発明は、
線状の放電極と、
その放電極を中心にして取り囲む筒状にされ、内周面に螺旋状の凹部が形成された対向電極と、
その筒状の対向電極の一端から他端へ空気が流通するように送風する送風手段と、
放電極と対向電極との間に電圧を印加して放電を発生し、空気中に含まれる被処理成分を対向電極に捕集させる電源と、
被処理成分を吸収する処理液を対向電極の内周面に供給する処理液供給手段と、
対向電極を軸回転させることにより、遠心力によって処理液を凹部へ一旦、溜め、その凹部から処理液を偏ることなく下方へ流下させる処理液均一化手段と、
を備えることを主要な特徴とする。
The second invention also provides
A linear discharge electrode;
A counter electrode having a cylindrical shape surrounding the discharge electrode and a spiral recess formed on the inner peripheral surface;
A blowing means for blowing air so that air flows from one end to the other end of the cylindrical counter electrode;
A power source that generates a discharge by applying a voltage between the discharge electrode and the counter electrode, and collects the component to be treated contained in the air in the counter electrode;
A treatment liquid supply means for supplying a treatment liquid that absorbs the component to be treated to the inner peripheral surface of the counter electrode;
A processing liquid homogenizing means for temporarily storing the processing liquid in the concave portion by centrifugal force by rotating the counter electrode, and flowing downward from the concave portion without biasing the processing liquid;
The main feature is to have

上記第2発明によると、放電極は線状であり、対向電極はその放電極を取り囲む筒状にされ、対向電極の内周面に螺旋状の凹部が形成されている。また、電源によって放電極と対向電極の間に電圧が印加され、放電が発生する。さらに、空気流通手段(例えばファン)によって対向電極の一端から他端へ空気が流通する。空気中に含まれる粒子状成分や気体状成分などの被処理成分は放電によって帯電して、対向電極に付着する。   According to the second aspect of the present invention, the discharge electrode is linear, the counter electrode is formed in a cylindrical shape surrounding the discharge electrode, and a spiral recess is formed on the inner peripheral surface of the counter electrode. In addition, a voltage is applied between the discharge electrode and the counter electrode by the power source to generate a discharge. Further, air is circulated from one end of the counter electrode to the other end by an air circulation means (for example, a fan). Processed components such as particulate components and gaseous components contained in the air are charged by discharge and adhere to the counter electrode.

一方、対向電極の内周面には、被処理成分を吸収する処理液(例えば水)が上方から供給される。また、対向電極は処理液均一化手段(例えばモータ)によって所定方向に軸回転しており、この回転によって遠心力が発生し、凹部に処理液が溜まるようになっている。その処理液は凹部にずっと溜まっているのではなく、少しずつ凹部から流出する。これにより、処理液が所定の部分に偏ることなく、対向電極の内周面を満遍なく濡らすことができる。また、使用する液量も少なくてすむ。   On the other hand, a treatment liquid (for example, water) that absorbs the component to be treated is supplied to the inner peripheral surface of the counter electrode from above. Further, the counter electrode is axially rotated in a predetermined direction by a processing liquid equalizing means (for example, a motor), and this rotation generates a centrifugal force so that the processing liquid is accumulated in the recess. The treatment liquid does not stay in the recess all the time, but gradually flows out of the recess. Thereby, the inner peripheral surface of the counter electrode can be evenly wetted without the treatment liquid being biased to a predetermined portion. Also, the amount of liquid used can be reduced.

さらに、本第3発明は、
線状の放電極と、
板状に形成され、所定間隔を空けて複数枚、配置されるとともに、放電極を間に位置させる対向電極と、
放電極と対向電極の間に空気を送る送風手段と、
対向電極と放電極の間に電圧を印加して放電を発生し、空気中に含まれる被処理成分を対向電極に捕集させる電源と、
被処理成分を吸収する処理液を対向電極に供給する処理液供給手段と、
対向電極を振動させることにより、処理液が偏らないようにする処理液均一化手段と、
を備えることを主要な特徴とする。
Furthermore, the third invention provides
A linear discharge electrode;
A counter electrode that is formed in a plate shape and is arranged with a plurality of predetermined intervals, with the discharge electrode positioned therebetween,
A blowing means for sending air between the discharge electrode and the counter electrode;
A power source that generates a discharge by applying a voltage between the counter electrode and the discharge electrode, and collects the component to be treated contained in the air in the counter electrode;
A processing liquid supply means for supplying a processing liquid that absorbs the component to be processed to the counter electrode;
Processing liquid homogenizing means for preventing the processing liquid from being biased by vibrating the counter electrode;
The main feature is to have

上記第3発明によると、対向電極は板状にされて複数枚、配置されており、その対向電極の間に線状の放電極が位置している。そして、放電極と対向電極の間に電圧を印加して、放電を発生させる。より詳しくは、対向電極は鉛直方向に向けられ、かつ互いに略平行に配置されており、上方から下方へ空気を送り、空気中の粉塵等を対向電極に付着させる。そして、対向電極の側面に水等の処理液を供給して、対向電極を湿潤状態にする。この対向電極は振動装置(処理液均一化手段)によって振動しており、これによって処理液の厚さが略均一に保たれる。   According to the third invention, a plurality of counter electrodes are arranged in a plate shape, and a linear discharge electrode is located between the counter electrodes. A voltage is applied between the discharge electrode and the counter electrode to generate a discharge. More specifically, the counter electrodes are oriented in the vertical direction and are arranged substantially parallel to each other, and air is sent from above to below to attach dust or the like in the air to the counter electrodes. Then, a treatment liquid such as water is supplied to the side surface of the counter electrode to wet the counter electrode. The counter electrode is vibrated by a vibration device (processing liquid uniformizing means), whereby the thickness of the processing liquid is kept substantially uniform.

また、本第4発明は、
放電極と、
対向電極と、
それら放電極および対向電極の間に空気を送る送風手段と、
放電極と対向電極の間に電圧を印加して放電を発生し、空気中に含まれる被処理成分を帯電させる電源と、
放電極および対向電極に対して空気の下流に配置され、帯電した被処理成分を捕集する集塵部と、
被処理成分を吸収する処理液を集塵部に供給する処理液供給手段と、
集塵部を動かすことにより、処理液が偏らないようにする処理液均一化手段と、
を備えることを主要な特徴とする。
Moreover, this 4th invention is
A discharge electrode;
A counter electrode;
A blowing means for sending air between the discharge electrode and the counter electrode;
A power source that generates a discharge by applying a voltage between the discharge electrode and the counter electrode, and charges the component to be treated contained in the air;
A dust collecting unit that is disposed downstream of the air with respect to the discharge electrode and the counter electrode, and collects charged components to be treated;
A processing liquid supply means for supplying a processing liquid that absorbs the component to be processed to the dust collecting section;
A processing liquid homogenizing means for preventing the processing liquid from being biased by moving the dust collecting section;
The main feature is to have

上記本第4発明によると、放電極と対向電極の間に放電を発生させ、かつ放電極と対向電極の間に空気を送るとともに、その空気の下流に集塵部を設けている。すなわち、空気中の被処理成分を帯電させるための放電極および対向電極を、集塵部と分けて配置している。これにより操作性がよくなる。集塵部は、例えば電極として構成され、電圧を印加することにより、帯電した粉塵等を捕集することができる。また、上記本第4発明によると、集塵部に処理液が供給されており、かつその集塵部が動いているので、集塵部の濡れ性を均一にできる。   According to the fourth aspect of the invention, the discharge is generated between the discharge electrode and the counter electrode, the air is sent between the discharge electrode and the counter electrode, and the dust collecting portion is provided downstream of the air. That is, the discharge electrode and the counter electrode for charging the component to be treated in the air are arranged separately from the dust collecting portion. This improves operability. The dust collecting unit is configured as an electrode, for example, and can collect charged dust and the like by applying a voltage. Further, according to the fourth aspect of the present invention, since the processing liquid is supplied to the dust collecting portion and the dust collecting portion is moving, the wettability of the dust collecting portion can be made uniform.

また、本第5発明は、上記第4発明におけるもので、
集塵部は筒状で、内周面に螺旋状の凹部が形成され、
処理液均一化手段は、対向電極を軸回転させることにより、遠心力によって処理液を凹部へ一旦、溜め、その凹部から処理液を偏ることなく下方へ流下させるものである。
Moreover, this 5th invention is in the said 4th invention,
The dust collection part is cylindrical, and a spiral recess is formed on the inner peripheral surface.
The processing liquid homogenizing means rotates the counter electrode axially, temporarily stores the processing liquid in the concave portion by centrifugal force, and causes the processing liquid to flow downward from the concave portion without being biased.

上記第5発明によると、本第2発明と同等の効果が得られる他、放電極および対向電極と、集塵部が別々に配置されているので、操作性が良くなるという効果も生じる。   According to the fifth aspect of the invention, the same effect as the second aspect of the invention can be obtained. In addition, since the discharge electrode and the counter electrode and the dust collecting part are separately disposed, the operability is improved.

さらに、本第6発明は、上記第4発明におけるもので、
対向電極は板状に形成され、所定間隔を空けて複数枚、配置され、
放電極は複数枚の対抗電極の間に位置し、
処理液均一化手段は、対向電極を振動させることにより、処理液が偏らないようにするものである。
Furthermore, this 6th invention is the said 4th invention,
The counter electrode is formed in a plate shape, a plurality of the electrodes are arranged at a predetermined interval,
The discharge electrode is located between a plurality of counter electrodes,
The processing liquid homogenizing means prevents the processing liquid from being biased by vibrating the counter electrode.

上記第6発明によると、本第3発明と同等の効果が得られる他、放電極および対向電極と、集塵部が別々に配置されているので、操作性が良くなるという効果も生じる。   According to the sixth invention, the same effect as that of the third invention can be obtained, and the discharge electrode, the counter electrode, and the dust collecting part are separately arranged, so that the operability is improved.

以下、本発明の実施形態を図面を参照しながら説明する。
図1Aは本発明に係る空気清浄機1の縦断面図であり、図1Bは同じく斜視図である。このように、空気清浄機1は線状の放電極2と、その放電極2を取り囲む筒状に構成され、内周面に螺旋状の凹部が形成された対向電極3を備える。対向電極3は両端が開口しており、上方が空気流入口9、下方が空気流出口10となっている。また、図示しない空気流通手段(ファン)を備え、空気を空気流入口9から空気流出口10へ送る。
Embodiments of the present invention will be described below with reference to the drawings.
FIG. 1A is a longitudinal sectional view of an air cleaner 1 according to the present invention, and FIG. 1B is a perspective view of the same. As described above, the air cleaner 1 includes the linear discharge electrode 2 and the counter electrode 3 which is configured in a cylindrical shape surrounding the discharge electrode 2 and has a spiral recess formed on the inner peripheral surface. Both ends of the counter electrode 3 are open, and the air inlet 9 is above and the air outlet 10 is below. In addition, an air circulation means (fan) (not shown) is provided to send air from the air inlet 9 to the air outlet 10.

一方、高電圧側電源5aおよび接地側電源5bによって、放電極2と対向電極3の間に電圧を加え、放電を発生させている。この放電によって空気中の粉塵やガス状成分が帯電して、対向電極3に引き寄せられる。また、処理液供給手段4(例えばポンプ)によって、対向電極3の内周面に処理液7(例えば水)を供給する。これによって、対向電極3に捕集された粉塵等を除去する。この処理液7は対向電極3の内周面を伝わって下方に流下し、装置下方に配置された水槽6に溜まる。その後、排水口11から排水され、処理液供給手段4によって汲み上げられて、対向電極3に再び供給される。装置を可動していると処理液7が汚れてくるので、汚れがあるレベル以上になったら交換する。   On the other hand, a voltage is applied between the discharge electrode 2 and the counter electrode 3 by the high voltage side power source 5a and the ground side power source 5b to generate a discharge. Due to this discharge, dust and gaseous components in the air are charged and attracted to the counter electrode 3. Further, the processing liquid 7 (for example, water) is supplied to the inner peripheral surface of the counter electrode 3 by the processing liquid supply means 4 (for example, a pump). As a result, dust or the like collected on the counter electrode 3 is removed. The treatment liquid 7 flows down along the inner peripheral surface of the counter electrode 3 and accumulates in a water tank 6 disposed below the apparatus. Thereafter, the water is drained from the drain port 11, pumped up by the processing liquid supply means 4, and supplied again to the counter electrode 3. When the apparatus is moved, the treatment liquid 7 becomes dirty, and is replaced when the level exceeds the level.

また、対向電極3の内周面には螺旋状の凹部Dが形成されている。対向電極3は、モータ8(処理液均一化手段の一例)によって所定方向に軸回転するようになっている。図2に、対向電極3の拡大図を示す。対向電極3が軸回転することによって遠心力が発生し、この遠心力と重力がつりあった状態で、処理液7が凹部Dに溜まる。凹部Dは螺旋状に形成してあるので、処理液7は重力によって凹部Dの中を下方へ流れる。また、遠心力はそれほど強くならないようにしてあり、対向電極3の内周面のうち、凹部Dの形成されていない領域Aへ向かって、凹部Dの中の処理液7が流出するようになっている。流出した処理液7は下方の凹部Dに入ることになる。   Further, a spiral recess D is formed on the inner peripheral surface of the counter electrode 3. The counter electrode 3 is axially rotated in a predetermined direction by a motor 8 (an example of a processing liquid uniformizing unit). FIG. 2 shows an enlarged view of the counter electrode 3. Centrifugal force is generated by rotating the counter electrode 3, and the treatment liquid 7 is accumulated in the recess D in a state where the centrifugal force and gravity are balanced. Since the recess D is formed in a spiral shape, the processing liquid 7 flows downward in the recess D by gravity. Further, the centrifugal force is not so strong, and the processing liquid 7 in the recess D flows out toward the region A where the recess D is not formed on the inner peripheral surface of the counter electrode 3. ing. The outflowing treatment liquid 7 enters the lower recess D.

以上説明したようにすることで、対向電極3の濡れ性を均一にすることができる。すなわち、凹部Dが形成されていない領域Aに、処理液7の液膜が略均一な厚さで形成され、この液膜は螺旋状の凹部Dのいたるところで流下するので、満遍なく濡れるのである。その結果、空気と処理液7との接触面積を増やすことができ、空気中の被処理成分の吸収効率が上がる。また、使用する処理液7の量も少なくてすむ。   As described above, the wettability of the counter electrode 3 can be made uniform. In other words, the liquid film of the treatment liquid 7 is formed in a substantially uniform thickness in the region A where the concave part D is not formed, and the liquid film flows down everywhere in the spiral concave part D, so that it gets wet evenly. As a result, the contact area between the air and the treatment liquid 7 can be increased, and the absorption efficiency of the component to be treated in the air is increased. Further, the amount of the treatment liquid 7 to be used can be reduced.

なお、図1の空気清浄機では対抗電極3として縦置きタイプのものを使用したが、横置きにしてもかまわない。この場合、処理液7が対抗電極3内を横向きに移動することになる。すなわち、対抗電極3の内面には螺旋状の凹部Dが形成されているので、その中に処理液7が入り、対抗電極3の回転に伴って処理液7が凹部D内を移動して排出口から出ていく。その途中で、凹部Dが形成されていない領域Aへ向かって処理液7が凹部Dから流出したり、滴下したりするので、対抗電極3の内面を均一に濡らすことが可能になる。なお、対抗電極3を水平面に対して角度をつけて斜めに配置し、上から処理液7を入れて対抗電極3を回転し、重力によって処理液7を流下させることもできるが、本発明では凹部Dが形成されているので、対抗電極3を完全に水平にしても処理液7を流通させることができる。   In addition, in the air cleaner of FIG. 1, although the vertical type thing was used as the counter electrode 3, you may make it horizontal. In this case, the treatment liquid 7 moves sideways in the counter electrode 3. That is, since the spiral recess D is formed on the inner surface of the counter electrode 3, the treatment liquid 7 enters therein, and the process liquid 7 moves through the recess D as the counter electrode 3 rotates. Go out from the exit. On the way, the processing liquid 7 flows out or drops from the recess D toward the region A where the recess D is not formed, so that the inner surface of the counter electrode 3 can be uniformly wetted. The counter electrode 3 may be disposed obliquely at an angle with respect to the horizontal plane, and the treatment liquid 7 may be poured from above by rotating the counter electrode 3 so that the treatment liquid 7 flows down by gravity. Since the recess D is formed, the treatment liquid 7 can be circulated even if the counter electrode 3 is completely horizontal.

次に、本発明の別の実施形態を図3に示す。図3の空気清浄機1は、板状の対向電極3が複数枚、略平行に配置されており、その間に線状の放電極2が位置している。これら対向電極3と放電極2の間に電圧を印加して、放電を発生する。一方、処理液供給手段4によって処理液7が対向電極3の上端から供給されて、対向電極3の表面は湿潤状態となる。対向電極3は図示しない振動発生機(処理液均一化手段の一例)によって振動され、これによって対向電極3の濡れ性が均一になる。   Next, another embodiment of the present invention is shown in FIG. In the air purifier 1 of FIG. 3, a plurality of plate-like counter electrodes 3 are arranged substantially in parallel, and the linear discharge electrode 2 is positioned therebetween. A voltage is applied between the counter electrode 3 and the discharge electrode 2 to generate a discharge. On the other hand, the processing liquid 7 is supplied from the upper end of the counter electrode 3 by the processing liquid supply means 4, and the surface of the counter electrode 3 becomes wet. The counter electrode 3 is vibrated by an unillustrated vibration generator (an example of a processing liquid uniformizing means), whereby the wettability of the counter electrode 3 becomes uniform.

さらに、図4A,Bに示すように、放電極2および対向電極3と、集塵部12を分離した2段式タイプにしてもよい。すなわち、空気は放電極2および対向電極3の間を通って、放電によって空気中の被処理成分が帯電し、それら放電極2と対向電極3に対して空気の下方に位置する集塵部12に、帯電した被処理成分が捕集される。このようにすると装置の操作性がよくなる。   Further, as shown in FIGS. 4A and 4B, a two-stage type in which the discharge electrode 2, the counter electrode 3, and the dust collecting portion 12 are separated may be used. That is, the air passes between the discharge electrode 2 and the counter electrode 3, and the component to be processed in the air is charged by the discharge, and the dust collector 12 located below the air with respect to the discharge electrode 2 and the counter electrode 3. In addition, the charged component to be treated is collected. This improves the operability of the apparatus.

なお、上記実施形態では対向電極3として円筒形や板状のものを使用したが、これらの形状は特に限定するものではなく、他には多角形状のもの等も電極形状として考えられる。また、設置形態に関しても縦置き、横置き等どのようにしてもよい。また、処理液を対向電極3へ供給する方法であるが、これについても特に限定するものではなく、対向電極の前段部分で噴霧・滴下したり、対向電極3の空気流入口9または側面から内壁へ注入路を介して直接導入してもよい。さらに、上記実施形態では対向電極3を回転する場合と振動させる場合についての実施形態を示したが、対抗電極3が動作して濡れ性が一様になるのであれば動作形態に限定はなく、例えば超音波等を利用した微小な振動でもよい。   In the above embodiment, a cylindrical or plate-like electrode is used as the counter electrode 3, but these shapes are not particularly limited, and other polygonal shapes can be considered as electrode shapes. In addition, the installation form may be set vertically or horizontally. Further, the processing liquid is supplied to the counter electrode 3. However, this is not particularly limited, and spraying and dripping is performed at the front stage portion of the counter electrode, or the inner wall from the air inlet 9 or the side surface of the counter electrode 3 is used. It may be introduced directly through the injection path. Furthermore, in the said embodiment, although embodiment about the case where the counter electrode 3 was rotated and the case where it vibrates was shown, if the counter electrode 3 operate | moves and wettability will become uniform, there will be no limitation in an operation | movement form, For example, minute vibrations using ultrasonic waves or the like may be used.

実験結果を示す。対向電極として直径300mm、長さ600mmの円筒形状のものを用い、かつその円筒管内部に水を供給して濡れ壁を形成した。また、対抗電極の中に線状の放電極を配置し、DC9kVの電圧を印加してコロナ放電を発生させた。そのコロナ放電にアンモニアガス(60ppm)を含む空気を送り、アンモニアガスの除去性能と水量の関係を調べた。   Experimental results are shown. A cylindrical electrode having a diameter of 300 mm and a length of 600 mm was used as the counter electrode, and water was supplied into the cylindrical tube to form a wet wall. Further, a linear discharge electrode was arranged in the counter electrode, and a voltage of DC 9 kV was applied to generate corona discharge. Air containing ammonia gas (60 ppm) was sent to the corona discharge, and the relationship between the ammonia gas removal performance and the amount of water was investigated.

その結果を図5に示す。対向電極3への供給する水の量が3.7L/min以上になると、水膜が略均一になることが分かった。そして、水量が1.0〜3.7L/minまではアンモニア除去率が水量に比例するのに対して、3.7L/min以上になるとアンモニア除去率が飽和することが分かった。すなわち、水量を3.7L/min以上に増やしても除去率は上がらず、水量が増えた分だけコストアップになる。これは、均一な液膜を形成できるなら、使用する水量を減らして、かつ処理性能を向上できることを意味する。   The result is shown in FIG. It was found that when the amount of water supplied to the counter electrode 3 was 3.7 L / min or more, the water film became substantially uniform. Then, it was found that the ammonia removal rate was proportional to the water amount up to 1.0 to 3.7 L / min, whereas the ammonia removal rate was saturated when the water amount was 3.7 L / min or more. That is, even if the amount of water is increased to 3.7 L / min or more, the removal rate does not increase, and the cost increases by the amount of increased water. This means that if a uniform liquid film can be formed, the amount of water used can be reduced and the treatment performance can be improved.

本発明に係る空気清浄機の(A)縦断面図(B)斜視図(A) longitudinal cross-sectional view (B) perspective view of an air cleaner according to the present invention 対向電極3の拡大図Enlarged view of counter electrode 3 空気清浄機の別の実施形態Another embodiment of the air purifier A図、B図とも、図1および3とは別の実施形態である。Both FIG. A and FIG. B are different embodiments from FIG. 1 and FIG. 実験結果Experimental result 従来例Conventional example

符号の説明Explanation of symbols

1 空気清浄機
2 放電極
3 対向電極
4 ポンプ(処理液供給手段)
5a,5b 電源
6 水槽
7 処理液
8 モータ(処理液均一化手段)
9 空気流入口
10 空気流出口
11 排水口
12 集塵部
DESCRIPTION OF SYMBOLS 1 Air cleaner 2 Discharge electrode 3 Counter electrode 4 Pump (process liquid supply means)
5a, 5b Power supply 6 Water tank 7 Treatment liquid 8 Motor (treatment liquid equalization means)
9 Air inlet 10 Air outlet 11 Drain outlet 12 Dust collector

Claims (6)

空気の流通経路上に配置された放電極と、
前記空気中に含まれる被処理成分を捕集する対向電極と、
前記被処理成分を吸収する処理液を前記対向電極に供給する処理液供給手段と、
前記対向電極を動かすことにより、前記処理液が偏らないようにする処理液均一化手段と、
を備えることを特徴とする空気清浄機。
A discharge electrode disposed on the air flow path;
A counter electrode for collecting the component to be treated contained in the air;
Treatment liquid supply means for supplying a treatment liquid that absorbs the component to be treated to the counter electrode;
A treatment liquid homogenizing means for preventing the treatment liquid from being biased by moving the counter electrode;
An air purifier characterized by comprising:
線状の放電極と、
その放電極を中心にして取り囲む筒状にされ、内周面に螺旋状の凹部が形成された対向電極と、
その筒状の対向電極の一端から他端へ空気が流通するように送風する送風手段と、
前記放電極と前記対向電極との間に電圧を印加して放電を発生し、前記空気中に含まれる被処理成分を前記対向電極に捕集させる電源と、
前記被処理成分を吸収する処理液を前記対向電極の内周面に供給する処理液供給手段と、
前記対向電極を軸回転させることにより、遠心力によって前記処理液を前記凹部へ一旦、溜め、その凹部から前記処理液を偏ることなく下方へ流下させる処理液均一化手段と、
を備えることを特徴とする空気清浄機。
A linear discharge electrode;
A counter electrode having a cylindrical shape surrounding the discharge electrode and a spiral recess formed on the inner peripheral surface;
A blowing means for blowing air so that air flows from one end to the other end of the cylindrical counter electrode;
A power source that generates a discharge by applying a voltage between the discharge electrode and the counter electrode, and causes the counter electrode to collect a component to be processed contained in the air;
Treatment liquid supply means for supplying a treatment liquid that absorbs the component to be treated to the inner peripheral surface of the counter electrode;
Processing liquid homogenizing means for temporarily storing the processing liquid in the concave portion by centrifugal force by rotating the counter electrode, and flowing down the processing liquid from the concave portion without being biased;
An air purifier characterized by comprising:
線状の放電極と、
板状に形成され、所定間隔を空けて複数枚、配置されるとともに、前記放電極を間に位置させる対向電極と、
前記放電極と前記対向電極の間に空気を送る送風手段と、
前記対向電極と前記放電極の間に電圧を印加して放電を発生し、前記空気中に含まれる被処理成分を前記対向電極に捕集させる電源と、
前記被処理成分を吸収する処理液を前記対向電極に供給する処理液供給手段と、
前記対向電極を振動させることにより、前記処理液が偏らないようにする処理液均一化手段と、
を備えることを特徴とする空気清浄機。
A linear discharge electrode;
A counter electrode that is formed in a plate shape and is disposed in a plurality at a predetermined interval, and the discharge electrode is positioned therebetween,
A blowing means for sending air between the discharge electrode and the counter electrode;
A power source that generates a discharge by applying a voltage between the counter electrode and the discharge electrode, and collects a component to be processed contained in the air in the counter electrode;
Treatment liquid supply means for supplying a treatment liquid that absorbs the component to be treated to the counter electrode;
A treatment liquid homogenizing means for preventing the treatment liquid from being biased by vibrating the counter electrode;
An air purifier characterized by comprising:
放電極と、
対向電極と、
それら放電極および対向電極の間に空気を送る送風手段と、
前記放電極と前記対向電極の間に電圧を印加して放電を発生し、前記空気中に含まれる被処理成分を帯電させる電源と、
前記放電極および前記対向電極に対して前記空気の下流に配置され、帯電した前記被処理成分を捕集する集塵部と、
前記被処理成分を吸収する処理液を前記集塵部に供給する処理液供給手段と、
前記集塵部を動かすことにより、前記処理液が偏らないようにする処理液均一化手段と、
を備えることを特徴とする空気清浄機。
A discharge electrode;
A counter electrode;
A blowing means for sending air between the discharge electrode and the counter electrode;
A power source that generates a discharge by applying a voltage between the discharge electrode and the counter electrode, and charges a component to be processed contained in the air;
A dust collecting unit that is disposed downstream of the air with respect to the discharge electrode and the counter electrode and collects the charged component to be treated;
A treatment liquid supply means for supplying a treatment liquid that absorbs the component to be treated to the dust collector;
A processing liquid homogenizing means for preventing the processing liquid from being biased by moving the dust collecting section;
An air purifier characterized by comprising:
前記集塵部は筒状で、内周面に螺旋状の凹部が形成され、
前記処理液均一化手段は、前記対向電極を軸回転させることにより、遠心力によって前記処理液を前記凹部へ一旦、溜め、その凹部から前記処理液を偏ることなく下方へ流下させる請求項4記載の空気清浄機。
The dust collection portion is cylindrical, and a spiral recess is formed on the inner peripheral surface,
5. The processing liquid homogenizing means temporarily stores the processing liquid in the concave portion by centrifugal force by rotating the counter electrode, and causes the processing liquid to flow downward from the concave portion without being biased. Air purifier.
前記対向電極は板状に形成され、所定間隔を空けて複数枚、配置され、
前記放電極は前記複数枚の対抗電極の間に位置し、
前記処理液均一化手段は、前記対向電極を振動させることにより、前記処理液が偏らないようにする請求項4記載の空気清浄機。
The counter electrode is formed in a plate shape, and a plurality of sheets are arranged at a predetermined interval,
The discharge electrode is located between the plurality of counter electrodes;
The air cleaner according to claim 4, wherein the processing liquid homogenizing unit vibrates the counter electrode to prevent the processing liquid from being biased.
JP2005080265A 2005-03-18 2005-03-18 Air cleaner Pending JP2006255662A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2005080265A JP2006255662A (en) 2005-03-18 2005-03-18 Air cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2005080265A JP2006255662A (en) 2005-03-18 2005-03-18 Air cleaner

Publications (1)

Publication Number Publication Date
JP2006255662A true JP2006255662A (en) 2006-09-28

Family

ID=37095445

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2005080265A Pending JP2006255662A (en) 2005-03-18 2005-03-18 Air cleaner

Country Status (1)

Country Link
JP (1) JP2006255662A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180047967A (en) * 2016-11-02 2018-05-10 씨에이티 주식회사 a seperator oil mist and moisture for COG
KR20190010676A (en) * 2019-01-11 2019-01-30 씨에이티 주식회사 Oil mist seperator
KR20210119117A (en) * 2020-03-24 2021-10-05 이앤엠 주식회사 Dust precipitator collecting dust particles by using an annular discharge region and dust precipitation system having the same
KR102347101B1 (en) * 2021-08-11 2022-01-06 주식회사 진에너텍 Hybrid wet electrostatic dust precipitator and slurry fueling system with the same

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180047967A (en) * 2016-11-02 2018-05-10 씨에이티 주식회사 a seperator oil mist and moisture for COG
KR101986815B1 (en) * 2016-11-02 2019-10-01 씨에이티 주식회사 a seperator oil mist and moisture for COG
KR20190010676A (en) * 2019-01-11 2019-01-30 씨에이티 주식회사 Oil mist seperator
KR102043674B1 (en) * 2019-01-11 2019-11-12 씨에이티 주식회사 Oil mist seperator
KR20210119117A (en) * 2020-03-24 2021-10-05 이앤엠 주식회사 Dust precipitator collecting dust particles by using an annular discharge region and dust precipitation system having the same
KR102448562B1 (en) * 2020-03-24 2022-09-29 이앤엠 주식회사 Dust precipitator collecting dust particles by using an annular discharge region and dust precipitation system having the same
KR102347101B1 (en) * 2021-08-11 2022-01-06 주식회사 진에너텍 Hybrid wet electrostatic dust precipitator and slurry fueling system with the same

Similar Documents

Publication Publication Date Title
KR101420508B1 (en) Wet electrostatic precipitator having ionizer and air purifying apparatus using the same
JP4894739B2 (en) Wet electric dust collector
KR101601246B1 (en) A air cleaner
KR101455570B1 (en) Wet electrostatic precipitator
KR101867373B1 (en) Collecting Electrode Washing Equipment And Wet Electrostatic Precipitator Using The Same
US20200047299A1 (en) Coolant recapture and recirculation in material removal systems
JP5040612B2 (en) Air purification device
KR101288217B1 (en) Wet Air Cleaning Apparatus
JPWO2009104411A1 (en) Dust collector
KR20120065650A (en) Moth-proof net having particle removing function
KR101622238B1 (en) A wet electrostatic precipitator, and a water-absorbent resin is applied to jipjinpan
JP2012125734A (en) Outside air processing device
KR101995742B1 (en) Wet Type Dust Collector Using Electrospray and Vortex
KR101502333B1 (en) Electricdust collector apparatus in electrostatic precipitator system and method for electrostatic precipitation thereby
KR101951185B1 (en) Liquid Spray Apparatus for Wet Type Dust Collector
KR101971917B1 (en) Dust Collector of Electrostatic Spray Device
JP2006255662A (en) Air cleaner
CN106999951B (en) Wet electrostatic precipitator and method for treating exhaust gas
JP2006102651A (en) Air cleaning apparatus
JP2008006371A (en) Dust collector
JP2015536241A (en) Electric dust collecting device provided in electric dust collecting system and dust collecting method using the electric dust collecting device
JP2004167453A (en) Dust collector
JP2010162430A (en) Suspended particulate matter removal apparatus
KR101778956B1 (en) Washer for recycling plastics
JP2012205974A (en) Electric dust collection device, and external air treatment device with the same

Legal Events

Date Code Title Description
A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20080212

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080414

RD04 Notification of resignation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7424

Effective date: 20080528