JPS6121715A - Particle flocculator - Google Patents
Particle flocculatorInfo
- Publication number
- JPS6121715A JPS6121715A JP14204884A JP14204884A JPS6121715A JP S6121715 A JPS6121715 A JP S6121715A JP 14204884 A JP14204884 A JP 14204884A JP 14204884 A JP14204884 A JP 14204884A JP S6121715 A JPS6121715 A JP S6121715A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- microparticles
- dust
- positive
- fine particles
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/017—Combinations of electrostatic separation with other processes, not otherwise provided for
- B03C3/0175—Amassing particles by electric fields, e.g. agglomeration
Landscapes
- Electrostatic Separation (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分i
本発明は集塵機における捕集効率の向上に寄与する粒子
凝集装置に関する。DETAILED DESCRIPTION OF THE INVENTION Industrial Application i The present invention relates to a particle aggregation device that contributes to improving collection efficiency in a dust collector.
従来例の構成とその問題点
従来、含塵ガスを導入して清浄ガスを放出する集塵機と
してはサイクロン式集塵機、電気集塵機、バグフィルタ
式集塵機などが知られている。これら集塵機は粗大粒子
であれば十分に捕集できるが、含塵ガス中に微細粒子が
ある場合には次のような問題が発生する。Conventional Structure and Problems Conventionally, cyclone type dust collectors, electric dust collectors, bag filter type dust collectors, etc. are known as dust collectors that introduce dust-containing gas and release clean gas. These dust collectors can sufficiently collect coarse particles, but if there are fine particles in the dust-containing gas, the following problems occur.
つまり、サイクロン式集塵機では微細粒子になると粗大
粒子の場合のように遠心力効果を期待できないため捕集
効率が極めて悪くなる。電気集塵機では微細′粒子の移
動度が非常に遅くて微細粒子まで捕集するためにはガス
流速を遅くし集塵機を大型化する必要があって、装置コ
ストが大変高いものとなつ′ている。また、バグフィル
タ式集塵機の場合にはフィルタの網目を極めて微細にす
る必 □要があり、このように網目を微細にすると圧力
損失が増大して運転コストが嵩むと云う難点を有してい
る。In other words, in a cyclone type dust collector, when the particles become fine, the centrifugal force effect cannot be expected as in the case of coarse particles, so the collection efficiency becomes extremely poor. In an electrostatic precipitator, the mobility of fine particles is very slow, and in order to collect even the fine particles, it is necessary to slow down the gas flow rate and increase the size of the dust collector, resulting in a very high equipment cost. In addition, in the case of a bag filter type dust collector, the mesh of the filter must be made extremely fine, which has the disadvantage that making the mesh so fine increases pressure loss and increases operating costs. .
このように従来の集塵機自体では低コストで微細粒子を
十分に捕集することが困難であるのが現状である。As described above, the current situation is that it is difficult to sufficiently collect fine particles at low cost using the conventional dust collector itself.
発明の目的
本発明は含塵ガス中の微細粒子を集塵機の前段で凝集粗
大化して、集塵機で微細粒子を取り扱わすとも済むよう
に作用する、構成が簡単な粒子凝集装置を提供すること
を目的とする。OBJECTS OF THE INVENTION The object of the present invention is to provide a particle agglomeration device with a simple structure, which functions by coagulating and coarsening fine particles in dust-containing gas before a dust collector so that the fine particles do not need to be handled by the dust collector. shall be.
発明の構成
本発明の粒子凝集装置は、正コロナ発生電極と負コロナ
発生電極を設け、この両電極に正負の高電圧を印加する
と共に両電極間に含塵ガスを導入して含塵ガス中の粒子
を合体凝集させるようにしたことを特徴とする。Structure of the Invention The particle agglomeration device of the present invention is provided with a positive corona generating electrode and a negative corona generating electrode, applies positive and negative high voltages to both electrodes, and introduces a dust-containing gas between the two electrodes to collect dust in the dust-containing gas. It is characterized by being made to coalesce and agglomerate the particles.
かかる構成によれば、導入した含塵ガス中の微細粒子を
(ト)と(→に帯電させることが出来、この帯電した両
微細粒子は相互間のクーロン力による吸引力によって合
体凝集して粗大化するため、微細粒子のない含塵ガスを
放出できる。従って、集塵機の前段に本発明の粒子凝集
装置を設置し、この粒子凝集装置を通した含塵ガスを集
塵機に導入することによって、微細粒子を伴った含塵ガ
スを従来の集塵機で効率よく処理することが出来、運転
費のコストダウンを達成できる。According to this configuration, it is possible to charge the fine particles in the introduced dust-containing gas to (T) and (→, and these charged fine particles coalesce and aggregate due to the attraction force due to the Coulomb force between them and become coarse. Therefore, by installing the particle agglomeration device of the present invention in the front stage of the dust collector and introducing the dust-containing gas through this particle aggregation device into the dust collector, it is possible to release dust-containing gas without fine particles. Dust-containing gas accompanied by particles can be efficiently treated with a conventional dust collector, and operating costs can be reduced.
実施例と作用
以下、本発明の一実施例を第1図〜第8図に基づいて説
明する。Embodiment and Function An embodiment of the present invention will be described below with reference to FIGS. 1 to 8.
第1図は本発明の粒子凝集装置の使用状態を示す。(1
)は集塵機、(2)は集塵機(1)の前段に設置された
粒子凝集装置で、微細粒子を伴った被処理含塵ガス流(
4)が導入され、この導入された被処理含塵ガス流(4
)を微細粒子を伴わない含塵ガス流(靭にして前記集塵
機(1)へ送り込むものである。(0は前記集塵機(1
)で粗大粒、子が捕集されて放出された清浄ガスを表わ
す。FIG. 1 shows the state in which the particle agglomeration device of the present invention is used. (1
) is a dust collector, and (2) is a particle agglomeration device installed before the dust collector (1).
4) is introduced, and this introduced dust-containing gas flow (4) is introduced.
) is made into a dust-containing gas flow (toughened) without fine particles and sent to the dust collector (1).
) represents the clean gas released after collecting coarse particles and particles.
第2図は粒子凝集装置(2)の基本構成を示す。(3)
と【4)は電極面を対向させて配設した正コロナ発生電
極と負コロナ発生電極で、何れも前記電極面には多数の
針状突起(5)が林立させである。(6) (7)は側
板で、前記電極(3) (4)とでガス通路を形成して
いる。FIG. 2 shows the basic configuration of the particle agglomeration device (2). (3)
and (4) are a positive corona generating electrode and a negative corona generating electrode which are arranged with their electrode surfaces facing each other, and both have a large number of needle-like protrusions (5) standing on the electrode surfaces. (6) and (7) are side plates, which form a gas passage with the electrodes (3) and (4).
なお、この側板(6) (7)を介して前記電極(3)
(4)間が電気的に短絡されないように側板(6)(
7)は絶縁体材料で形成するか、電極(3) (4)と
側板(6) (7)との間に絶縁物〔図示せず〕を介装
して十分な絶縁耐力を保証している。(8J (9)は
高圧電源への接続線を表わしている。Note that the electrode (3) is connected to the electrode (3) through this side plate (6) (7).
(4) Side plate (6) (
7) is made of an insulating material, or an insulator (not shown) is interposed between the electrode (3) (4) and the side plate (6) (7) to ensure sufficient dielectric strength. There is. (8J (9) represents the connection line to the high voltage power supply.
このように構成したため、接続線(8) (9)を介し
て電極(3) (4)を高圧電源σ1に接続するとコロ
ナ放電が発生して電極(3)からは(イ)イオンが、電
極(4)からは(→イオンが放出され、第8図のように
して被処理含塵ガス流囚が微細粒子を伴わない含塵ガス
流(旬に処理される。つまり、コロナ放電が発生すると
第8図(a)のように前記微細粒子のうちの電極(3)
の近傍の微細粒子(G1)には(→イオンが付着して(
→に帯電し、電極(4)の近傍の微細粒子(G2)には
←)イオンが付着して(→に帯電する。(→に帯電した
微細粒子(G1)は電極(4)側に引かれて移動し、(
→に帯電した微細粒子(Gりは電極(3)側に引かれて
移動し、この移動の途中で帯電した微細粒子(G、)と
(G2)が遭遇し、両者はクーロン力によって吸引し合
って第8図(b)の(ト)のように合体する。この際、
微細粒子が導電体であれば合体によって放電して合体粒
子(ト)には(ト)電荷と(→電荷の帯電量の差分の電
荷が残る。帯電量が等しい場合には電荷は零となる。な
お、微細粒子が非導電体の場合には一部の電荷は放電す
ることもあるが、大部分は当初の電荷を保ったまま合体
粒子(ハ)となって合体後も相互の微細粒子(Gl)
(G2) の(ト)電荷と(→電荷が吸引として作用
して凝集力を高める効果が得られる。但し、この場合の
合体粒子(0の見かけ上の電荷の帯電量は当初の微細粒
子(Gl)(G2)の電荷の帯電量の差となり、電荷猷
が等しいときは零となる。With this configuration, when the electrodes (3) and (4) are connected to the high-voltage power supply σ1 via the connecting wires (8) and (9), corona discharge occurs and (a) ions are emitted from the electrode (3). From (4), (→ ions are released, and as shown in Figure 8, the dust-containing gas to be treated is treated as a dust-containing gas flow without fine particles. In other words, when corona discharge occurs, As shown in FIG. 8(a), the electrode (3) of the fine particles
(→ ions are attached to the fine particles (G1) in the vicinity of (
The fine particles (G2) near the electrode (4) are charged with →, and ions are attached to them (←) and charged with →. The fine particles (G1) charged with → are attracted to the electrode (4) side. He moved and moved (
→ The charged fine particles (G) are attracted to the electrode (3) and move, and during this movement, the charged fine particles (G,) and (G2) encounter each other, and the two are attracted by Coulomb force. and merge as shown in (g) in Figure 8(b).At this time,
If the fine particles are conductive, they discharge due to coalescence, and the combined particles (g) retain a charge equal to the difference between the charges (g) and (→charge). If the charges are equal, the charge becomes zero. Note that if the fine particles are non-conductive, some of the charge may be discharged, but most of them retain their initial charge and become coalesced particles (c), and even after coalescing, the fine particles continue to dissipate from each other. (Gl)
(G2)'s (g) charge and (→ charge act as attraction and have the effect of increasing the cohesive force. However, in this case, the amount of apparent charge of the coalesced particle (0) is smaller than that of the initial fine particle ( This is the difference in the amount of charge between Gl) and (G2), and becomes zero when the charges are equal.
上記のように合体した合体粒子(ト)にも、第8図(C
)のように再び(ト)イオン、(→イ′オンが付着して
帯電するため、上記の帯電した微細粒子(Gl) (G
2) の場合と同様に合体粒子(lのうちの電極(3〉
近傍にあって(→に帯電した合体粒子(Dl)は電極(
4)側に引かれて移動し、電極(4)近傍にあって(→
に帯電した合体粒子(D2)は電極(3)側に引かれて
移動する。この合体粒子(D、)”と(D2)は第8図
(d)のように途中で逆極性に帯電した粒子に遭遇し、
クーロン力によって相互に引き合って(P4)のように
合体凝集する。合体後の粒子の電荷の帯電状態は微細粒
子(Gl) (G、)の場合と同様である。Figure 8 (C
), the (g) ions and (→ ions) attach and become electrically charged, so the charged fine particles (Gl) (G
2) As in the case of the combined particle (electrode (3) of l)
A coalesced particle (Dl) near the electrode (→) is charged to the electrode (
4) and moves near the electrode (4) (→
The charged combined particles (D2) are attracted to the electrode (3) and move. These combined particles (D, )'' and (D2) encounter oppositely charged particles on the way, as shown in Figure 8(d).
They are attracted to each other by Coulomb force and coalesce and aggregate as shown in (P4). The charged state of the particles after coalescence is the same as that of the fine particles (Gl) (G,).
このような第8図(a)〜(d)を繰り返しながら粒子
は合体凝集し粗大化して行く。While repeating the steps shown in FIGS. 8(a) to 8(d), the particles coalesce, aggregate, and become coarser.
なお、上記実施例では電極(3) (4)の電極面には
針状突起(5)を設けてコロナ放電が容易に発生するよ
うに構成したm゛、これは針状突起(5ンに代って襞状
の突起体としても同様の効果を期待できる。In the above embodiment, needle-like protrusions (5) were provided on the electrode surfaces of the electrodes (3) and (4) to facilitate the generation of corona discharge. The same effect can be expected by using a pleated projection instead.
発明の詳細
な説明のように本発明の粒子凝集装置は、正コロナ発生
電極と負コロナ発生電極を設け、この両電極に正負の直
電圧を印加すると共に両電極間に含塵ガスを導入するよ
うにしたため、コロナ放電で発生した←)イオンと(→
イオンが導入された含塵ガス中の微細粒子に付着して(
ト)に帯電した微細粒子と(→に帯電した微細粒子とが
それぞれ正コロナ電極近傍と負コロナ電極近傍に発生し
、帯電した微細粒子が対向電極に向って移動する途中で
逆極性に帯電した粒子とクーロン力で引き合って合体し
て次第に粗大粒子化し、微細粒子を伴った含塵ガス流を
構成簡単にして微細粒子を伴わない含塵ガス流に処理し
て放出することができる。このような粒子凝集装置を集
塵機の前後に設置した場合には、微細粒子が凝集粗大化
されて捕集しやすくなり集塵機では粗大化粒子の捕集を
実行して微細粒子の捕集を考慮せずとも済むため、本発
明の粒子凝集装置は集塵装置全体のコストダウンと運転
コストの低減化に寄与できるものである。As described in the detailed description of the invention, the particle aggregation device of the present invention is provided with a positive corona generating electrode and a negative corona generating electrode, applying positive and negative direct voltages to both electrodes, and introducing dust-containing gas between the two electrodes. As a result, ←) ions generated by corona discharge and (→
Ions adhere to fine particles in the introduced dust-containing gas (
Fine particles charged to (g) and (→) are generated near the positive corona electrode and near the negative corona electrode, respectively, and the charged fine particles are charged to opposite polarities while moving toward the counter electrode. The particles are attracted by the Coulomb force and coalesce, gradually becoming coarse particles, and a dust-containing gas flow with fine particles can be easily constructed, processed into a dust-containing gas flow without fine particles, and released. If a particle agglomeration device is installed before and after the dust collector, the fine particles will be aggregated into coarse particles, making it easier to collect, and the dust collector will collect the coarse particles without considering the collection of fine particles. Therefore, the particle aggregation device of the present invention can contribute to reducing the cost of the entire dust collector and the operating cost.
第1図は本発明の粒子凝集装置の使用状態説明図、第2
図は本発明の粒子凝集装置の一実施例の要部斜視図、第
8図は微細粒子凝集過程の説明図である。Figure 1 is an explanatory diagram of the usage state of the particle agglomeration device of the present invention, Figure 2
The figure is a perspective view of essential parts of an embodiment of the particle aggregation device of the present invention, and FIG. 8 is an explanatory diagram of the fine particle aggregation process.
Claims (1)
両電極に正負の高電圧を印加すると共に両電極間に含塵
ガスを導入して含塵ガス中の粒子を合体凝集させるよう
にした粒子凝集装置。1. A positive corona generating electrode and a negative corona generating electrode were provided, and positive and negative high voltages were applied to both electrodes, and a dust-containing gas was introduced between the two electrodes to cause particles in the dust-containing gas to coalesce and agglomerate. Particle agglomeration device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14204884A JPS6121715A (en) | 1984-07-09 | 1984-07-09 | Particle flocculator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14204884A JPS6121715A (en) | 1984-07-09 | 1984-07-09 | Particle flocculator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6121715A true JPS6121715A (en) | 1986-01-30 |
Family
ID=15306187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14204884A Pending JPS6121715A (en) | 1984-07-09 | 1984-07-09 | Particle flocculator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6121715A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6336870A (en) * | 1986-07-31 | 1988-02-17 | Juki Corp | Micro-discharge device for liquid |
JP2001253524A (en) * | 2000-03-15 | 2001-09-18 | Juki Corp | Substrate carrier device of chip mounter |
KR20020069864A (en) * | 2001-02-28 | 2002-09-05 | 한국기계연구원 | Structure of a collecting plate for a dust collector |
-
1984
- 1984-07-09 JP JP14204884A patent/JPS6121715A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6336870A (en) * | 1986-07-31 | 1988-02-17 | Juki Corp | Micro-discharge device for liquid |
JPH0425074B2 (en) * | 1986-07-31 | 1992-04-28 | Juki Kk | |
JP2001253524A (en) * | 2000-03-15 | 2001-09-18 | Juki Corp | Substrate carrier device of chip mounter |
KR20020069864A (en) * | 2001-02-28 | 2002-09-05 | 한국기계연구원 | Structure of a collecting plate for a dust collector |
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