TW202012047A - Electric dust collector - Google Patents

Electric dust collector Download PDF

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TW202012047A
TW202012047A TW108128957A TW108128957A TW202012047A TW 202012047 A TW202012047 A TW 202012047A TW 108128957 A TW108128957 A TW 108128957A TW 108128957 A TW108128957 A TW 108128957A TW 202012047 A TW202012047 A TW 202012047A
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discharge
electrode
dust
dust collecting
collecting electrode
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TWI742415B (en
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富松一隆
加藤雅也
上田泰稔
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日商三菱日立電力系統環保股份有限公司
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/08Plant or installations having external electricity supply dry type characterised by presence of stationary flat electrodes arranged with their flat surfaces parallel to the gas stream
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/06Plant or installations having external electricity supply dry type characterised by presence of stationary tube electrodes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/36Controlling flow of gases or vapour
    • B03C3/361Controlling flow of gases or vapour by static mechanical means, e.g. deflector
    • B03C3/366Controlling flow of gases or vapour by static mechanical means, e.g. deflector located in the filter, e.g. special shape of the electrodes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/40Electrode constructions
    • B03C3/41Ionising-electrodes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/40Electrode constructions
    • B03C3/45Collecting-electrodes
    • B03C3/47Collecting-electrodes flat, e.g. plates, discs, gratings
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/40Electrode constructions
    • B03C3/45Collecting-electrodes
    • B03C3/49Collecting-electrodes tubular
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C2201/00Details of magnetic or electrostatic separation
    • B03C2201/10Ionising electrode has multiple serrated ends or parts
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C2201/00Details of magnetic or electrostatic separation
    • B03C2201/14Details of magnetic or electrostatic separation the gas being moved electro-kinetically

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Abstract

Provided is an electric dust collector that can effectively collect dust even at a dust collecting electrode on the side opposite to a corona discharge unit. The invention comprises: a discharge electrode (5) that has a main unit (5b) and a projection (5a) for corona discharge projecting from the main unit (5b); a discharge side dust collecting electrode (4a) that is located on the projection (5a) side; and an opposite side dust collecting electrode (4b) that is located on the side opposite to the discharge side dust collecting electrode (4a) with the discharge electrode (5) therebetween; wherein the center (C1) of the main unit (5b) of the discharge electrode (5) is located further from the discharge side dust collecting electrode (4a) than the central position (CL) between the discharge side dust collecting electrode (4a) and the opposite side dust collecting electrode (4b).

Description

電集塵裝置Electric dust collector

本發明係關於一種電集塵裝置者。The invention relates to an electric dust collector.

作為先前之電集塵裝置,已知有具備沿氣流平行排列之平板狀之集塵極、及排列於其中央之具有電暈放電部之放電極者。對於放電極之電暈放電部之形狀,存在藉由具有突起形狀使電場集中而確保電暈放電之方式之使放電極本體產生同樣之電場集中的構造,例如角線或細鋼琴線等,但於一般產業用電集塵裝置中,即便電極污染,亦確保穩定之電暈放電,因而以具有突起狀之電暈放電部之構造為主流,且以下以該構造為前提。As a conventional electric dust collector, a plate-shaped dust collector electrode arranged in parallel along the air flow and a discharge electrode having a corona discharge part arranged at the center thereof are known. Regarding the shape of the corona discharge part of the discharge electrode, there is a structure in which the discharge electrode body generates the same concentration of the electric field by having a protruding shape to concentrate the electric field to ensure the corona discharge, such as a corner line or a thin piano wire, but In general industrial dust collectors, even if the electrodes are contaminated, a stable corona discharge is ensured. Therefore, a structure having a protruding corona discharge portion is the mainstream, and this structure is assumed as a premise below.

電集塵裝置中,藉由對集塵極與放電極間施加直流高電壓,於放電極之電暈放電部進行穩定之電暈放電,而使氣流中之灰塵帶電。於先前之集塵理論中說明了帶電之灰塵藉由於放電極與集塵極間之電場下作用於灰塵之庫侖力之動作而被集塵極捕集。In the electric dust collecting device, by applying a high DC voltage between the dust collecting electrode and the discharge electrode, a stable corona discharge is carried out at the corona discharge part of the discharge electrode to charge the dust in the airflow. The previous dust collection theory explained that charged dust is trapped by the dust collector due to the action of the Coulomb force acting on the dust under the electric field between the discharge electrode and the dust collector.

然而,專利文獻1、2之電集塵裝置具備:集塵極,其具備用以使灰塵通過之複數個貫通孔,且具有用以將灰塵捕集至內部之封閉空間。於專利文獻1、2中,藉由將灰塵經由該貫通孔封閉於封閉空間,而使捕集灰塵不易再飛散。However, the electric dust collectors of Patent Documents 1 and 2 include a dust collector, which has a plurality of through holes for passing the dust, and a closed space for trapping the dust inside. In Patent Documents 1 and 2, the enclosed dust is sealed in the closed space through the through hole, so that the collected dust is not easily scattered.

專利文獻3之電集塵裝置具備:集塵極,其包含具有65%至85%之開口率之接地電極、及捕集氣體之集塵過濾層。藉由具備此種集塵極,而於專利文獻3中,於與氣流正交之剖面內產生離子風,且生成於放電極與集塵極間循環之螺旋狀之氣流,並高效地捕集灰塵。於專利文獻3中,雖積極地利用離子風,但本實例之目的主要在於以集塵過濾層捕集灰塵。 [先前技術文獻] [專利文獻]The electric dust collector of Patent Document 3 includes a dust collector including a ground electrode having an opening ratio of 65% to 85%, and a dust collection filter layer for trapping gas. By having such a dust collecting electrode, in Patent Document 3, ion wind is generated in a cross section orthogonal to the air flow, and a spiral air flow circulating between the discharge electrode and the dust collecting electrode is generated and efficiently collected dust. In Patent Document 3, although ion wind is actively used, the purpose of this example is mainly to collect dust with a dust collection filter layer. [Prior Technical Literature] [Patent Literature]

[專利文獻1]日本專利特許第5761461號公報 [專利文獻2]日本專利特許第5705461號公報 [專利文獻3]日本專利特許第4823691號公報[Patent Document 1] Japanese Patent Publication No. 5671461 [Patent Document 2] Japanese Patent Publication No. 5705461 [Patent Document 3] Japanese Patent Publication No. 4823691

[發明所欲解決之問題][Problems to be solved by the invention]

電集塵裝置之集塵效率η可藉由熟知之下述多依奇算式(式(1))算出。w係集塵性指數(粒子狀物質之移動速度),f係每單位氣體量之集塵面積。

Figure 02_image001
The dust collection efficiency η of the electric dust collector can be calculated by the following well-known odd formula (equation (1)). w is the dust collection index (movement speed of particulate matter), and f is the dust collection area per unit gas volume.
Figure 02_image001

上述式(1)中,灰塵(粒子狀物質)之移動速度w由庫倫力之力與氣體之粘性電阻之關係決定。多依奇算式(上述式(1))中,設為灰塵自放電極移動於電場內,未直接考慮離子風對性能之影響。然而,其性能設計之前提即灰塵濃度之分佈通常以於與電集塵裝置之氣流正交之放電極與集塵極間之集塵空間之剖面內相同為前提條件,且認為離子風係使氣體產生混亂,且使灰塵濃度相同之主要原因之一。In the above formula (1), the moving speed w of dust (particulate matter) is determined by the relationship between the force of the Coulomb force and the viscosity resistance of the gas. In the multi-odd formula (formula (1) above), it is assumed that dust moves from the discharge electrode in the electric field, and the effect of ion wind on performance is not directly considered. However, before the performance design, it is mentioned that the distribution of dust concentration is usually based on the same premise as the cross section of the dust collecting space between the discharge electrode and the dust collecting electrode orthogonal to the airflow of the electric dust collecting device. One of the main reasons why the gas is chaotic and the dust concentration is the same.

離子風係對電極間施加負電壓時,藉由放電極之電暈放電產生負離子,且以此為結果而產生者,於正電壓之情形時,藉由正離子產生。以下,本說明書中,因將產業用電集塵裝置視為基礎,故對施加負電壓之實例進行記載,正電壓之情形亦同樣。When a negative voltage is applied between the electrodes by the ion wind system, negative ions are generated by the corona discharge of the discharge electrode, and those generated as a result are generated by positive ions in the case of positive voltage. In the following, in this specification, industrial electric dust collectors are taken as the basis, so examples of applying negative voltages are described, and the same applies to positive voltages.

沿氣流配置有電極群之電集塵裝置中,由放電極產生之離子風以朝向集塵極橫穿氣流之方式流動。到達集塵極之離子風由集塵極反轉,而改變流動方向。藉此,於電極間產生螺旋狀之亂流。In an electric dust collecting device with electrode groups arranged along the airflow, the ion wind generated by the discharge electrode flows in a manner crossing the airflow toward the dust collecting electrode. The ion wind reaching the dust collecting pole is reversed by the dust collecting pole, and the flow direction is changed. As a result, a spiral turbulent flow is generated between the electrodes.

亂流中,自放電極朝向集塵極之流動有將灰塵送至集塵極附近之作用。送至集塵極附近之灰塵最終由庫倫力捕集。In the turbulent flow, the flow from the discharge electrode toward the dust collecting electrode has the effect of sending the dust to the vicinity of the dust collecting electrode. The dust sent to the dust collecting pole is finally collected by Coulomb.

然而,以集塵極反轉之離子風使灰塵朝向遠離收集體即集塵極之方向移動,故亦有如阻礙集塵之作用。因此,於集塵極設置開口部,防止離子風反轉之方式較為有效。However, the ion wind reversed by the dust-collecting pole moves the dust in a direction away from the collecting body, that is, the dust-collecting pole, so it also acts as a hindrance to dust collection. Therefore, it is more effective to provide an opening in the dust collecting pole to prevent the ion wind from reversing.

於專利文獻3中,記載有亦考慮離子風之效果之電集塵裝置。然而,該實例中為對位於具有開口部之集塵極之背後之過濾層送入離子風的構造,其目的在於,於不受主氣體影響之部位進行集塵,且構造亦複雜,於乾式作業時難以剝離回收附著之灰塵。Patent Document 3 describes an electric dust collector that also considers the effect of ion wind. However, in this example, the structure for sending ion wind to the filter layer behind the dust collecting electrode with an opening is aimed at collecting dust at a location not affected by the main gas, and the structure is also complicated, and is dry. It is difficult to peel off and collect attached dust during operation.

又,藉由自放電極之本體部突出之電暈放電部所產生之電暈放電,而使離子風隨電暈電流一起向集塵極側流動,但於放電極中與未設置電暈放電部之相反側之集塵極間,因未產生電暈放電,故無法利用離子風。又,於未設置電暈放電部之相反側,電暈電流或帶電灰塵之集塵空間之電荷量與電暈放電部相比較少,因而集塵極附近之電場強度之上升與電暈放電部側相比較少,庫倫力之集塵作用亦變弱。因此,本發明者等著眼於積極地利用電暈放電部之相反側之集塵極。In addition, the corona discharge generated by the corona discharge part protruding from the body part of the discharge electrode causes the ion wind to flow to the dust collecting electrode side along with the corona current, but the discharge electrode is not provided with corona discharge Between the dust-collecting poles on the opposite side of the part, the ion wind cannot be used because there is no corona discharge. In addition, on the opposite side of the area where the corona discharge part is not provided, the corona current or the amount of charge in the dust collecting space of the charged dust is less than that of the corona discharge part, so the increase in the electric field strength near the dust collecting pole and the corona discharge part The dust collection effect of the Coulomb force is also weakened compared to the side. Therefore, the inventors focused on actively using the dust collecting electrode on the opposite side of the corona discharge part.

本發明係鑑於此種情況而完成者,其目的在於提供一種電暈放電部之相反側之集塵極亦可有效集塵之電集塵裝置。 [解決問題之技術手段]The present invention has been completed in view of such circumstances, and its object is to provide an electric dust collector that can effectively collect dust on the opposite side of the corona discharge part. [Technical means to solve the problem]

本發明之一態樣之電集塵裝置具備:放電極,其具有本體部及自該本體部突出之電暈放電用之電暈放電部;放電側集塵極,其位於上述電暈放電部側;及相反側集塵極,其隔著上述放電極位於上述放電側集塵極之相反側;且上述放電極之上述本體部之中心位於較上述放電側集塵極與上述相反側集塵極間之中央位置更靠向遠離上述放電側集塵極之方向。An electric dust collector according to an aspect of the present invention includes: a discharge electrode having a body portion and a corona discharge portion for corona discharge protruding from the body portion; a discharge side dust collector electrode located at the corona discharge portion Side; and the opposite side dust collector electrode, which is located on the opposite side of the discharge side dust collector electrode through the discharge electrode; and the center of the body portion of the discharge electrode is located more than the discharge side dust collector electrode and the opposite side dust collector The central position between the electrodes is further away from the above-mentioned discharge side dust collecting electrode.

放電極具有僅向集塵極中之一者之放電側集塵極突出之電暈放電部。藉此,可自電暈放電部僅向放電側集塵極電暈放電,並使離子風流動。該方式與通常之放電極中藉由於兩側具有電暈放電部而使離子風於兩側流動之方式相比,有可使與隔著集塵極相對之放電極間之離子風之干涉消失之優點。 然而,隔著放電極位於放電側集塵極之相反側,即電暈放電部之相反側之相反側集塵極因不與電暈放電部對向,故幾乎不產生電暈放電。然而,因放電極之本體部之中心較放電側集塵極與相反側集塵極間之中央位置位於更遠離放電側集塵極之方向,故放電極之本體部與相反側集塵極接近。藉此,可增加放電極之本體部與相反側集塵極間之電場強度,且於相反側電極中亦因庫侖力之提高而可提高集塵效率。 放電極之本體部之中心例如於放電側集塵極與相反側集塵極間之距離為300 mm以上500 mm以下之情形時,較佳離開相反側集塵極側10 mm以上而定位。 作為集塵極,例如列舉將複數個具有剛性之構件以特定間隔排列之離散形集塵極。作為具有剛性之構件,例如列舉本體部為導管形狀之構件。又,作為其他形式之集塵極,例如列舉設為具有複數個貫通孔之板狀體之平板集塵極。作為平板集塵極,使用例如衝孔金屬或金屬網。The discharge electrode has a corona discharge portion that protrudes only toward the discharge side dust collecting electrode of one of the dust collecting electrodes. Thereby, the corona discharge from the corona discharge part only to the discharge side dust collecting electrode can cause the ion wind to flow. This method can make the interference of the ion wind between the discharge electrode opposed to the dust collector electrode disappear due to the flow of ion wind on both sides due to the corona discharge parts on both sides of the common discharge electrode. Advantage. However, the dust collecting electrode located on the opposite side of the discharge side dust collecting electrode via the discharge electrode, that is, the opposite side of the corona discharge part, does not face the corona discharge part, so that corona discharge hardly occurs. However, since the center of the body portion of the discharge electrode is located further away from the discharge side dust collection electrode than the center position between the discharge side dust collection electrode and the opposite side dust collection electrode, the body portion of the discharge electrode is close to the opposite side dust collection electrode . In this way, the electric field strength between the body portion of the discharge electrode and the dust collecting electrode on the opposite side can be increased, and the dust collection efficiency can also be improved in the electrode on the opposite side due to the increase in Coulomb force. The center of the body portion of the discharge electrode is preferably positioned more than 10 mm away from the opposite side of the dust collecting electrode when the distance between the discharge side dust collecting electrode and the opposite side dust collecting electrode is 300 mm or more and 500 mm or less, for example. As the dust collecting electrode, for example, a discrete-type dust collecting electrode in which a plurality of rigid members are arranged at specific intervals is cited. As a member having rigidity, for example, a member whose body portion is in the shape of a catheter is cited. In addition, as another type of dust collecting electrode, for example, a flat plate dust collecting electrode provided with a plate-like body having a plurality of through holes is cited. As the flat dust collector, for example, punched metal or metal mesh is used.

再者,本發明之一態樣之電集塵裝置中,將上述放電極之上述本體部之中心與上述放電側集塵極間之距離設為D1,將上述放電極之上述本體部之中心與上述相反側集塵極間之距離設為D2之情形時,設為1.1≦D1/D2≦2.0。Furthermore, in an electric dust collector of one aspect of the present invention, the distance between the center of the body portion of the discharge electrode and the discharge side dust collection electrode is D1, and the center of the body portion of the discharge electrode When the distance from the dust collecting electrode on the opposite side is D2, it is set to 1.1≦D1/D2≦2.0.

藉由設為1.1≦D1/D2≦2.0,而可增加放電極之本體部與相反側集塵極間之電場強度,且使該電場強度接近電暈放電部與電極側集塵極間之電場強度。與1.1>D1/D2之情形相比,集塵性能提高,與D1/D2>2.0之情形不同,可防止火花放電之產生。By setting 1.1≦D1/D2≦2.0, the electric field strength between the body part of the discharge electrode and the opposite side dust collecting electrode can be increased, and the electric field strength can be made close to the electric field between the corona discharge part and the electrode side dust collecting electrode strength. Compared with the case of 1.1>D1/D2, the dust collection performance is improved. Unlike the case of D1/D2>2.0, it can prevent the occurrence of spark discharge.

再者,本發明之一態樣之電集塵裝置中,上述放電側集塵極與上述相反側集塵極分別沿一方向排列,上述D1為上述放電極之本體部之中心與上述放電側集塵極之排列位置間之距離,上述D2為上述放電極之本體部之中心與上述相反側集塵極之排列位置間之距離。Furthermore, in an electric dust collector of one aspect of the present invention, the discharge side dust collection electrode and the opposite side dust collection electrode are arranged in one direction, respectively, and the D1 is the center of the body portion of the discharge electrode and the discharge side The distance between the arrangement positions of the dust collecting electrodes, D2 is the distance between the center of the body portion of the discharge electrode and the arrangement position of the opposite dust collecting electrodes.

放電側集塵極與相反側集塵極分別沿一方向排列,D1為相對於放電側集塵極之排列方向,於垂直方向中放電極之本體部之中心與放電側集塵極之排列位置間之距離,D2為相對於相反側集塵極之排列方向,於垂直方向中放電極之本體部之中心與相反側集塵極之排列位置間之距離。The discharge-side dust-collecting electrode and the opposite-side dust-collecting electrode are respectively arranged in one direction, D1 is the arrangement direction relative to the discharge-side dust-collecting electrode, the center of the body of the discharge electrode and the discharge-side dust-collecting electrode are arranged in the vertical direction The distance between them, D2 is the distance between the center of the body of the discharge electrode and the arrangement position of the opposite dust collecting pole in the vertical direction relative to the arrangement direction of the opposite dust collecting pole.

再者,本發明之一態樣之電集塵裝置中,上述放電極與上述放電側集塵極間之電場強度、與上述放電極與上述相反側集塵極間之電場強度相等。Furthermore, in an electric dust collector of one aspect of the present invention, the electric field strength between the discharge electrode and the discharge side dust collector electrode is equal to the electric field strength between the discharge electrode and the opposite side dust collector electrode.

藉由使放電極與放電側集塵極間之電場強度、與放電極與相反側集塵極間之電場強度相等,而可較將放電極之本體部之中心定位於兩集塵極間之中央之情形,增加放電極與相反側電極間之電場強度。By making the electric field strength between the discharge electrode and the discharge side dust collecting electrode equal to the electric field strength between the discharge electrode and the opposite side dust collecting electrode, the center of the body of the discharge electrode can be positioned between the two dust collecting electrodes In the center, increase the electric field strength between the discharge electrode and the electrode on the opposite side.

再者,本發明之一態樣之電集塵裝置中,上述電暈放電部之前端位於較上述放電側集塵極與上述相反側集塵極間之上述中央位置更靠向上述相反側集塵極側。Furthermore, in an electric dust collector of one aspect of the present invention, the front end of the corona discharge portion is located closer to the opposite side than the center position between the discharge side dust collecting electrode and the opposite side dust collecting electrode Dust pole side.

藉由使電暈放電部之前端位於較兩集塵極間之中央位置更靠向相反側集塵極側,而可降低電暈放電部與放電側集塵極間之電場強度,且增加放電極之本體部與相反側電極間之電場強度。 [發明之效果]By making the front end of the corona discharge part closer to the opposite side of the dust collecting electrode than the central position between the two dust collecting electrodes, the electric field strength between the corona discharge part and the discharge side dust collecting electrode can be reduced and the discharge can be increased The electric field strength between the body of the electrode and the electrode on the opposite side. [Effect of invention]

藉由增加放電極之本體部與相反側集塵極間之電場強度,可於相反側電極中亦藉由庫倫力之提高而提高集塵效率,即便為相反側集塵極,亦可進而有效地集塵。By increasing the electric field strength between the body of the discharge electrode and the opposite side dust collecting electrode, the dust collecting efficiency can be improved by the improvement of the Coulomb force in the opposite side electrode, even if it is the opposite side dust collecting electrode, it can be further effective To collect dust.

以下,針對本發明之電集塵裝置之一實施形態,參照圖式進行說明。Hereinafter, an embodiment of the electric dust collector of the present invention will be described with reference to the drawings.

電集塵裝置1用於例如將煤等作為燃料之火力發電設備,回收自鍋爐導出之燃料排氣中之灰塵(粒子狀物質)。又,電集塵裝置1之各構成要件之尺寸與火力發電設備用不同,設置於建築物或地下空間等,回收微小粒子狀物質(例如PM2.5等),淨化空間內之空氣。The electric dust collector 1 is used for, for example, coal-fired thermal power generation equipment to collect dust (particulate matter) in fuel exhaust gas discharged from a boiler. In addition, the size of each component of the electric dust collector 1 is different from that of thermal power generation equipment. It is installed in a building or underground space, etc., and collects fine particulate matter (such as PM2.5, etc.) to purify the air in the space.

電集塵裝置1具備例如金屬製等之導電性之複數個集塵極4。集塵極4設為具有圓形橫剖面之中空柱狀之圓形導管,於與長度方向即z方向正交之x方向(氣流G方向)空開特定間隔而排列。排列於x方向之集塵極4之行於與z方向及x方向正交之y方向空開特定間隔而平行地設置有複數行。於集塵極4之各行間,於x-z面內配置有放電極5。於圖1中,顯示有放電極5之安裝框5c之位置。由圖1可知,放電極5自與氣流G方向正交之y方向上排列之集塵極4間之中央位置CL向一者之集塵極4側(圖1中為y方向之右側)偏移。The electric dust collector 1 includes a plurality of conductive dust collector electrodes 4 made of metal, for example. The dust collecting pole 4 is a circular duct having a hollow cylindrical shape with a circular cross section, and is arranged at a predetermined interval in the x direction (air flow G direction) orthogonal to the z direction, which is the longitudinal direction. The rows of the dust-collecting poles 4 arranged in the x direction are arranged in parallel at a certain interval in the y direction orthogonal to the z direction and the x direction, and are arranged in parallel. Between each row of the dust collecting electrode 4, a discharge electrode 5 is arranged in the x-z plane. In FIG. 1, the position of the mounting frame 5c of the discharge electrode 5 is shown. As can be seen from FIG. 1, the discharge electrode 5 is deviated from the central position CL between the dust collecting electrodes 4 arranged in the y direction orthogonal to the air flow G direction to one of the dust collecting electrodes 4 side (the right side in the y direction in FIG. 1) shift.

集塵極4接地。放電極5連接於未圖示之具有負極性之電源。另,連接於放電極5之電源亦可具有正極性。The dust collector 4 is grounded. The discharge electrode 5 is connected to a power source having a negative polarity (not shown). In addition, the power source connected to the discharge electrode 5 may also have a positive polarity.

如圖2所示,放電極5具備固定於安裝框5c之本體部5b、及自本體部5b突出之刺狀之複數個突起部(電暈放電部)5a。突起部5a設置為僅於一者之集塵極4側朝前端突出。突起部5a配置為於氣流G方向即x方向上,位於集塵極4之間。於突起部5a中產生電暈放電,自突起部5a之前端朝對向之集塵極4側產生離子風。As shown in FIG. 2, the discharge electrode 5 includes a body portion 5b fixed to the mounting frame 5c, and a plurality of protruding portions (corona discharge portions) 5a protruding from the body portion 5b. The protrusion 5a is provided so as to protrude toward the front end only on the dust collecting electrode 4 side of one. The protrusion 5a is arranged between the dust collecting pole 4 in the x direction of the air flow G direction. A corona discharge is generated in the protrusion 5a, and ion wind is generated from the front end of the protrusion 5a toward the opposing dust collecting electrode 4 side.

如圖2所示,放電極5之本體部5b之中心C1自集塵極4間之中央位置CL偏移。具體而言,放電極5之本體部5b之中心C1以於遠離突起部5a所對向之集塵極4(以下,將該集塵極4稱為「放電側集塵極4a」)之方向、且接近突起部5a之相反側之集塵極4(以下,將該集塵極4稱為「相反側集塵極4b」)之方式,自中央位置CL移位。因此,沿本體部5b之中心C1與通過放電側集塵極4a之中心C2之排列位置間之y方向觀察之距離D1,大於沿本體部5b之中心C1與通過相反側集塵極4b之中心C3之排列位置間之y方向觀察之距離D2(D1>D2)。另,由於放電極5及集塵極4於y方向交替配置,故1個集塵極4中,突起部5a側為放電側集塵極4a,突起部5a之相反側為相反側集塵極4b。As shown in FIG. 2, the center C1 of the body portion 5 b of the discharge electrode 5 is offset from the center position CL between the dust collecting electrodes 4. Specifically, the center C1 of the body portion 5b of the discharge electrode 5 is away from the dust collecting electrode 4 facing the protrusion 5a (hereinafter, this dust collecting electrode 4 is referred to as "discharge side dust collecting electrode 4a") And, it is displaced from the central position CL so as to approach the dust collecting electrode 4 on the opposite side of the protrusion 5a (hereinafter, this dust collecting electrode 4 is referred to as "the opposite side dust collecting electrode 4b"). Therefore, the distance D1 viewed along the y direction between the center C1 of the main body portion 5b and the center C2 passing through the discharge side dust collecting electrode 4a is greater than the center C1 along the main body portion 5b and the center passing through the opposite side dust collecting electrode 4b The distance D2 (D1>D2) observed in the y direction between the arrangement positions of C3. In addition, since the discharge electrode 5 and the dust collecting electrode 4 are alternately arranged in the y direction, in one dust collecting electrode 4, the protruding portion 5a side is the discharge side dust collecting electrode 4a, and the opposite side of the protruding portion 5a is the opposite side dust collecting electrode 4b.

距離D1係放電極5之本體部5b之中心C1與通過放電側集塵極4a之中心C2之排列位置間之距離。即,D1係於相對於放電側集塵極4a之排列方向垂直之方向(y方向)上,放電極5之本體部5b之中心C1與放電側集塵極4a之排列位置(中心軸線)間之距離。The distance D1 is the distance between the arrangement position of the center C1 of the body portion 5b of the discharge electrode 5 and the center C2 of the dust collecting electrode 4a passing through the discharge side. That is, D1 is between the center C1 of the main body portion 5b of the discharge electrode 5 and the arrangement position (center axis) of the discharge side dust collector 4a in a direction perpendicular to the arrangement direction of the discharge side dust collector 4a Distance.

距離D2係放電極5之本體部5b之中心C1與通過相反側集塵極4b之中心C3之排列位置間之距離。即,D2係於相對於相反側集塵極4b之排列方向垂直之方向(y方向)上,放電極5之本體部5b之中心C1與相反側集塵極4b之排列位置(中心軸線)間之距離。The distance D2 is the distance between the center C1 of the body portion 5b of the discharge electrode 5 and the arrangement position of the center C3 passing through the dust collecting electrode 4b on the opposite side. That is, D2 is between the center C1 of the main body portion 5b of the discharge electrode 5 and the arrangement position (center axis) of the opposite side dust collecting electrode 4b in a direction (y direction) perpendicular to the arrangement direction of the opposite side dust collecting electrode 4b Distance.

突起部5a之前端配置為,例如當放電極5之本體部5b之中心至放電部前端之距離、即Dd/2+Lb(參照圖4B)設為未達30 mm、較佳為20 mm左右之情形時,位於較中央位置CL更靠向相反側集塵極4b側。The front end of the protrusion 5a is arranged, for example, when the distance from the center of the body portion 5b of the discharge electrode 5 to the front end of the discharge portion, that is, Dd/2+Lb (see FIG. 4B) is set to less than 30 mm, preferably about 20 mm In this case, it is located closer to the opposite side of the dust collecting electrode 4b than the center position CL.

如上所述,因將突起部5a朝向一方向,且於x方向上配置於集塵極4之間,從而自突起部5a朝向放電側集塵極4a之離子風朝向大致相同方向,可避免離子風之干涉。As described above, since the protrusions 5a are oriented in one direction and are arranged between the dust collecting electrodes 4 in the x direction, the ion wind from the protrusions 5a toward the discharge side dust collecting electrodes 4a is oriented in substantially the same direction, which can avoid ions Wind interference.

圖3係顯示自氣流G方向觀察圖1之前視圖。如該圖所示,突起部5a於高度方向上空開特定間隔而設置。Fig. 3 is a front view of Fig. 1 viewed from the direction of the air flow G. As shown in the figure, the protrusions 5a are provided at specific intervals in the height direction.

圖4A係顯示俯視集塵極4與放電極5時之位置關係。 將排列於氣流G方向即x方向之集塵極4之間隔設為Pc,將排列於x方向之放電極5之間隔設為Pd。又,將排列於y方向之集塵極4之間隔設為2D。將集塵極4之直徑設為Dc。4A shows the positional relationship when the dust collecting electrode 4 and the discharge electrode 5 are viewed from above. Let the interval of the dust collecting electrodes 4 arranged in the x direction of the airflow G be Pc, and the interval of the discharge electrodes 5 arranged in the x direction be Pd. In addition, the interval between the dust collecting electrodes 4 arranged in the y direction is set to 2D. Let the diameter of the dust collecting electrode 4 be Dc.

本實施形態中,放電極5之偏移位置,即放電極5之本體部5b之中心自中央位置CL朝y方向移位之位置,較佳將距離D1與距離D2之比設定為1.1≦D1/D2≦2.0之範圍內。D1/D2之下限設定為1.2更佳。In this embodiment, the offset position of the discharge electrode 5, that is, the position where the center of the body portion 5b of the discharge electrode 5 is displaced from the central position CL in the y direction, it is preferable to set the ratio of the distance D1 to the distance D2 to 1.1≦D1 /D2≦2.0. It is better to set the lower limit of D1/D2 to 1.2.

將放電極5之突起部5a之前端與最近之放電側集塵極4a之側面之距離設為L1,將放電極5之突起部5a之相反側之本體部5b與最近之相反側集塵極4b之側面之距離設為L2。 另,圖4A所示之放電極5與集塵極4間所描繪之曲線為電力線。The distance between the front end of the protrusion 5a of the discharge electrode 5 and the side surface of the nearest discharge side dust collecting electrode 4a is set to L1, and the body portion 5b on the opposite side of the protrusion 5a of the discharge electrode 5 and the nearest opposite dust collecting electrode The distance between the sides of 4b is set to L2. In addition, the curve drawn between the discharge electrode 5 and the dust collecting electrode 4 shown in FIG. 4A is a power line.

圖4B中放大顯示有與放電極5之突起部5a相當之高度位置之橫剖面。如同圖所示,放電極5之本體部5b具有圓形剖面,其直徑設為Dd。突起部5a自本體部5b突出之突起長度設為Lb。FIG. 4B shows an enlarged cross-section of a height position corresponding to the protrusion 5a of the discharge electrode 5. As shown in the figure, the body portion 5b of the discharge electrode 5 has a circular cross section, and its diameter is set to Dd. The length of the protrusion of the protrusion 5a protruding from the body 5b is set to Lb.

若使用圖4A及圖4B所示之參數,則L1及L2可如下式般表示。

Figure 02_image003
且,放電極5之本體部5b之中心自中央位置CL向y方向移位之偏移量Le由下式表示。
Figure 02_image005
另,圖4A及圖4B中顯示有刺狀之突起部5a之位置之剖面之例,但實際上突起部5a所佔部分為放電極5之一部分,相鄰二個突起部5a間之部分佔放電極5之大部分。因此,亦可忽視突起部5a之長度Lb而評估L1、L2。If the parameters shown in FIGS. 4A and 4B are used, L1 and L2 can be expressed as follows.
Figure 02_image003
Moreover, the offset Le of the center of the body portion 5b of the discharge electrode 5 displaced from the central position CL in the y direction is expressed by the following formula.
Figure 02_image005
In addition, FIGS. 4A and 4B show an example of a cross section of the position of the thorn-shaped protrusion 5a, but actually the portion occupied by the protrusion 5a is a part of the discharge electrode 5, and the portion between the two adjacent protrusions 5a Most of the discharge electrode 5. Therefore, the length Lb of the protrusion 5a can be ignored and L1 and L2 can be evaluated.

排列於y方向之集塵極4間之距離2D例如於一般產業用時設為300 mm以上500 mm以下。但於其他用途中,亦可設為其他尺寸。The distance 2D between the dust collecting electrodes 4 arranged in the y direction is set to 300 mm or more and 500 mm or less for general industrial use, for example. However, in other applications, it can also be set to other sizes.

其次,使用圖5A至圖6B,對使放電極5偏移之情形之作用效果進行說明。Next, the effect of the case where the discharge electrode 5 is shifted will be described using FIGS. 5A to 6B.

圖5A及圖5B中顯示有偏移量Le=0之無偏移之情形時,即,放電極5之本體部5b設置於中央位置CL上之情形之電場強度分佈。如圖5A所示,突起部5a與放電側集塵極4a之間隨著電暈電流流動,放電側集塵極4a附近之電場強度E1max因存在於空間中之負離子及帶電灰塵具有之空間電荷而上升。該放電側集塵極4a附近之火花放電界限之電場強度(Ecr)成為最大可施加之最大電場強度之條件(E1max≦Ecr)。FIGS. 5A and 5B show the electric field intensity distribution when there is no offset with the offset Le=0, that is, when the body portion 5b of the discharge electrode 5 is disposed at the central position CL. As shown in FIG. 5A, the corona current flows between the protruding portion 5a and the discharge-side dust collecting electrode 4a, and the electric field intensity E1max near the discharge-side dust collecting electrode 4a is due to the negative ions existing in the space and the space charge of the charged dust And rise. The electric field intensity (Ecr) of the spark discharge limit near the discharge side dust collecting electrode 4a becomes the condition of the maximum applied maximum electric field intensity (E1max≦Ecr).

另一方面,如圖5B所示,由於突起部5a之相反側與相反側集塵極4b間,無如圖5A般之因空間電荷之上升,故相反側集塵極4b附近之電場強度E2max小於E1max。 另,將電場強度以距離L1、L2積分之面積A1、A2因分別相當於施加電壓Vo,故變為相等值。On the other hand, as shown in FIG. 5B, since there is no increase in space charge as shown in FIG. 5A between the opposite side of the protruding portion 5a and the opposite side dust collecting electrode 4b, the electric field intensity E2max near the opposite side dust collecting electrode 4b Less than E1max. In addition, the areas A1 and A2 that integrate the electric field strength with the distances L1 and L2 correspond to the applied voltage Vo, respectively, and thus become equal values.

圖6A及圖6B中顯示有與本實施形態相當,且放電極5自中央位置CL偏移之情形之放電極5與集塵極4間之電場強度分佈。圖6A與圖5A對應,圖6B與圖5B對應。6A and 6B show the electric field intensity distribution between the discharge electrode 5 and the dust collecting electrode 4 corresponding to the present embodiment, and in the case where the discharge electrode 5 is shifted from the central position CL. 6A corresponds to FIG. 5A, and FIG. 6B corresponds to FIG. 5B.

如圖6A及圖6B所示,突起部5a與放電側集塵極4a間之電場強度因偏移而成為L1>L2或D1>D2,故若放電側集塵極4a附近之電場強度E1max為與無偏移之情形相同之電壓Vo,則進而較圖5A降低,且E1ave.(=Vo/L1)亦變小。另一方面,因偏移,L2較圖5B之情形更小,平均電場強度E2ave.變大,可使相反側集塵極4b附近之電場強度E2max增加。As shown in FIGS. 6A and 6B, the electric field strength between the protruding portion 5a and the discharge side dust collecting electrode 4a becomes L1>L2 or D1>D2 due to the offset, so if the electric field intensity E1max near the discharge side dust collecting electrode 4a is The voltage Vo, which is the same as the case without offset, is further lower than that in FIG. 5A, and E1ave. (=Vo/L1) also becomes smaller. On the other hand, due to the offset, L2 is smaller than in the case of FIG. 5B, and the average electric field strength E2ave. becomes larger, which can increase the electric field strength E2max near the opposite dust collecting electrode 4b.

一般而言,運轉時之E1max小於火花放電界限電場強度Ecr,但因偏移,突起物側之距離變長,故與無偏移之情形相比,其電場強度變得與最初之E1max相同,因而可提高施加線壓Vn本身(Vn>Vo),且與突起物相反側之最大電場強度E2max亦可進而提高。如此,藉由於偏移之同時提高施加電壓,而將電場強度E1max維持為與偏移前相等,且將E2max提高至與E1max相同之位準,藉此可提高集塵極附近集塵效果最佳之部位之電場強度,並提高依據庫倫力之捕集效率。另,由於偏移,電暈放電側之距離變大,於其間移動之灰塵之移動距離變大,但該部分之灰塵之移動主要依靠離子風,故到達距離之略微增加或中途之平均電場強度之降低不會對性能造成負面影響,且可因繞行至放電側集塵極4a之背側之相反側集塵極4b之灰塵之相反側集塵極4b附近之電場強度E2max之增大而提高性能。Generally speaking, the E1max during operation is less than the spark discharge limit electric field strength Ecr, but the distance on the protrusion side becomes longer due to the offset, so the electric field strength becomes the same as the original E1max compared to the case without offset. Therefore, the applied line voltage Vn itself (Vn>Vo) can be increased, and the maximum electric field intensity E2max on the side opposite to the protrusion can be further increased. In this way, by increasing the applied voltage while shifting, the electric field strength E1max is maintained equal to that before the shift, and E2max is increased to the same level as E1max, thereby improving the dust collection effect near the dust collector. The electric field strength of the part and improve the collection efficiency according to the Coulomb force. In addition, due to the offset, the distance of the corona discharge side becomes larger, and the moving distance of the dust moving between them becomes larger, but the movement of the dust in this part mainly depends on the ion wind, so the reaching distance slightly increases or the average electric field strength in the middle The reduction will not negatively affect the performance, and may be due to the increase in the electric field strength E2max near the opposite side dust collecting electrode 4b of the dust bypassing the dust collecting electrode 4b on the back side of the discharge side dust collecting electrode 4a Improve performance.

偏移量Le較佳調整為,使放電側集塵極4a之電場強度E1max及相反側集塵極4b之電場強度E2max相等。圖5A至圖6B所示之電場強度之例係空開間隔配置有導管狀之集塵極4之事例,以L1、L2之最短距離為基礎加以記載。因作為集塵極4之電極例,亦存在網眼狀之電極等,故以下為定義偏移量,而以通過集塵極4之中心C2、C3之排列位置與放電極5之中心C1間距離即D1、D2一併記述。該情形時,即便為導管狀之電極,即便以D1、D2而非L1、L2加以評估,於實用範圍內亦可視為大致相等,因而不存在障礙。The offset Le is preferably adjusted so that the electric field intensity E1max of the discharge side dust collecting electrode 4a and the electric field intensity E2max of the opposite side dust collecting electrode 4b are equal. The examples of the electric field intensity shown in FIGS. 5A to 6B are examples in which the duct-shaped dust collecting electrodes 4 are arranged at intervals, and are described based on the shortest distances of L1 and L2. As an example of the electrode of the dust collecting electrode 4, there are mesh-shaped electrodes, etc., so the following is the defined offset, and the arrangement position passing through the centers C2, C3 of the dust collecting electrode 4 and the center C1 of the discharge electrode 5 The distances, D1 and D2, are described together. In this case, even if it is a catheter-shaped electrode, even if it is evaluated by D1, D2 instead of L1, L2, it can be regarded as approximately equal in the practical range, so there is no obstacle.

兩者之電場強度相等之範圍例如為1.5≦D1/D2≦1.8。但,最佳之D1/D2之範圍根據電集塵裝置1之運轉條件或集塵極4或放電極5之條件而變動。The range in which the electric field strengths of the two are equal is, for example, 1.5≦D1/D2≦1.8. However, the optimal range of D1/D2 varies according to the operating conditions of the electric dust collector 1 or the conditions of the dust collecting electrode 4 or the discharge electrode 5.

距離D1及距離D2之比D1/D2之下限例如為1.1,更佳為1.2。如圖10所示,獲得偏移量與集塵性能之關係根據氣流G之流速而變化之見解。氣流G比較快時,若D1/D2變為1.1以上,則集塵性能提高。氣流G比較慢時,若D1/D2變為1.2以上,則集塵性能提高,於該範圍內,氣流G比較快時,集塵性能確實提高。The lower limit of the ratio D1/D2 between the distance D1 and the distance D2 is, for example, 1.1, and more preferably 1.2. As shown in FIG. 10, the insight that the relationship between the offset and the dust collection performance changes according to the flow velocity of the air flow G is obtained. When the airflow G is relatively fast, if D1/D2 becomes 1.1 or more, the dust collection performance is improved. When the airflow G is relatively slow, if D1/D2 becomes 1.2 or more, the dust collection performance is improved, and within this range, when the airflow G is relatively fast, the dust collection performance is indeed improved.

氣流G之流速較快之條件下,由於庫倫力之影響更大,故電場強度之增大受到影響,即便較小之偏移量(例如1.1≦D1/D2),集塵性能亦提高。相對於此,流速較慢之條件下,由於離子風之影響較大,故集塵性能因電場強度之增大而提高,需要更大之偏移量(例如1.2≦D1/D2)。若1.2≦D1/D2,則無關氣流G之流速,而可提高集塵性能。Under the condition that the flow rate of the airflow G is faster, the increase in the electric field strength is affected due to the greater Coulomb force. Even with a small offset (for example, 1.1≦D1/D2), the dust collection performance is also improved. On the contrary, under the condition of slow flow velocity, the influence of ion wind is greater, so the dust collection performance is improved due to the increase of the electric field strength, and a larger offset is required (for example, 1.2≦D1/D2). If 1.2≦D1/D2, the dust collection performance can be improved regardless of the flow rate of the airflow G.

若偏移量過大,則相反側集塵極附近之電場強度變為E2max>E1max,與電暈放電部相反側之火花放電界限電場強度成為運轉上之制約條件,無法發揮電暈放電側之性能,因而不佳。藉此,較佳為將最大偏移量設定於E2max不較大地超出E1max之範圍內。If the offset is too large, the electric field strength near the dust collecting electrode on the opposite side becomes E2max>E1max, and the electric field strength of the spark discharge limit on the opposite side of the corona discharge part becomes the operational constraint, and the performance on the corona discharge side cannot be exerted , Which is not good. Therefore, it is preferable to set the maximum offset within a range where E2max does not greatly exceed E1max.

圖11係顯示一般產業用電集塵裝置1中,對使D1/D2變化時之電暈放電側(於放電極5之本體部5b具有突起部5a之側,即,放電線有刺之側)之放電側集塵極4a附近之電場強度、與電場側(於放電極5之本體部5b不具有突起部5a之側,即,無刺之側)之相反側集塵極4b附近之電場強度進行解析並比較之例。使作為電集塵裝置1之運轉條件之電流電壓一同上升。圖11中,隨著自左圖表向右圖表進行,電流電壓變高。FIG. 11 shows the corona discharge side when the D1/D2 is changed in the general industrial electric dust collector 1 (the side where the body 5b of the discharge electrode 5 has the protrusion 5a, that is, the side where the discharge line is thorny ) The electric field strength near the discharge side dust collecting electrode 4a and the electric field side near the dust collecting electrode 4b on the opposite side of the electric field side (the side where the body portion 5b of the discharge electrode 5 does not have the protrusion 5a, ie, the non-thorn side) Examples of strength analysis and comparison. The current and voltage which are the operating conditions of the electric dust collector 1 are raised together. In FIG. 11, as the graph from left to right progresses, the current voltage becomes higher.

任一情形下,於D1/D2=1之情形時,不但有刺側之放電側集塵極4a因其刺之長度故而距離較近,再加上因電暈電流之空間電荷而使電場上升之效果,故而有刺側之放電側集塵極4a之電場強度較高。且,隨著電流增加,其上升效果變大,電場強度值變高。In any case, when D1/D2=1, not only the discharge side dust collector 4a on the thorn side is closer due to the length of the thorn, but also the electric field rises due to the space charge of the corona current As a result, the electric field intensity of the discharge side dust collecting electrode 4a on the barbed side is high. Moreover, as the current increases, its rising effect becomes larger, and the electric field intensity value becomes higher.

另一方面,圖11之任一圖表之情形亦顯示隨著D1/D2增加,無刺側之相反側集塵極4b之電場強度統一增加之傾向。理想而言,認為有刺側與無刺側之電場強度一致之點為最平衡之電場強度分配。然而於實際運轉中,由於複合了各種條件,故最佳條件有所變動。因此,使圖10之D1/D2變化時之集塵性提高之相關測試結果中,即便為集塵性能之最佳點,亦具有某種程度之偏差。On the other hand, the situation in any of the graphs in FIG. 11 also shows that as D1/D2 increases, the electric field intensity of the dust collecting electrode 4b on the opposite side of the non-barbed side increases uniformly. Ideally, the point where the electric field strength on the barbed side and the non-barbed side coincide is the most balanced distribution of electric field strength. However, in actual operation, due to the combination of various conditions, the optimal conditions have changed. Therefore, in the test results related to the improvement of the dust collection performance when D1/D2 in FIG. 10 is changed, even if it is the optimal point of the dust collection performance, there is a certain degree of deviation.

又,於圖11之右側圖表、即使電流電壓上升之運轉中,尤其在偏移量較大之D1/D2較大之區域內,無刺側之相反側集塵極4b會先超出一般產業用電集塵裝置1之火花放電電場強度(雖因氣體之組成或運轉溫度條件而有大幅差異,但通常設為8 kV/cm~12 kV/cm),因而不佳。 更具體而言,較佳設為D1/D2≦2.0。In addition, in the graph on the right side of FIG. 11, even when the current and voltage increase, especially in the area with a large offset D1/D2, the dust collector 4b on the opposite side of the non-barbed side will first exceed the general industrial use. The electric field intensity of the spark discharge of the electric dust collector 1 (although there is a large difference depending on the composition of the gas or the operating temperature condition, it is usually set to 8 kV/cm to 12 kV/cm), which is not good. More specifically, it is preferably D1/D2≦2.0.

若D1/D2超出2.0,則相反側集塵極4b側之電場強度於電集塵裝置1之通常運轉條件下,達到產生火花放電之區域,或接近達到值。因此,受電集塵裝置1之運轉條件之制約而難以穩定運轉。因此,較佳將D1/D2之上限設為2.0。If D1/D2 exceeds 2.0, the electric field intensity on the opposite side of the dust collecting electrode 4b reaches the area where spark discharge occurs under normal operating conditions of the electric dust collecting device 1, or close to the reached value. Therefore, it is difficult to operate stably due to the restriction of the operating conditions of the electric dust collector 1. Therefore, it is preferable to set the upper limit of D1/D2 to 2.0.

接著,說明本實施形態之電集塵裝置1之動作。 電集塵裝置1中,藉由自電源對放電極5施加負電極,而於突起部5a之前端產生電暈放電。氣流G所含之灰塵藉由電暈放電而帶電。以先前之電集塵裝置之捕集原理,帶電之灰塵因庫倫力而被吸引至接地之集塵極4,且被捕集於集塵極4上,但實際而言,離子風之影響發揮了較大之作用。Next, the operation of the electric dust collector 1 of this embodiment will be described. In the electric dust collector 1, by applying a negative electrode to the discharge electrode 5 from a power source, a corona discharge is generated at the front end of the protrusion 5a. The dust contained in the airflow G is charged by corona discharge. According to the previous collection principle of the electric dust collector, the charged dust is attracted to the grounded dust collector 4 due to the Coulomb force, and is trapped on the dust collector 4, but in reality, the influence of ion wind exerts A greater effect.

若產生電暈放電,則於突起部5a附近產生負離子,該負離子藉由電場而向集塵極4移動,產生離子風。因此,庫倫力作用於灰塵之同時,向集塵極4流動之離子風以使氣流G所含之灰塵移動至放電側集塵極4a附近之方式作用。且,於放電側集塵極4a附近之區域,藉由電場強度之上升而提高庫倫力,有效地將灰塵集塵。又,將作為圓形導管之集塵極4於特定之氣流G方向即x方向空開間隔配置,從而容許自突起部5a向放電側集塵極4a流動之離子風之一部分向集塵極4之背側逸出。藉此,可抑制離子風於集塵極4反轉而背離之流動,故捕集效率提高。When a corona discharge occurs, negative ions are generated in the vicinity of the protrusion 5a, and the negative ions move toward the dust collecting electrode 4 by an electric field to generate ion wind. Therefore, while the Coulomb force acts on the dust, the ion wind flowing toward the dust collecting electrode 4 acts so that the dust contained in the air flow G moves to the vicinity of the discharge side dust collecting electrode 4a. In addition, in the area near the dust collecting electrode 4a on the discharge side, the Coulomb force is increased by the increase of the electric field strength, and the dust is effectively collected. In addition, the dust collecting electrode 4 which is a circular duct is arranged at a certain air flow direction G, that is, in the x direction with a space therebetween, so that a part of the ion wind flowing from the protrusion 5a to the discharge side dust collecting electrode 4a is allowed to reach the dust collecting electrode 4 The back side escapes. As a result, the flow of ion wind that reverses and deviates from the dust collecting electrode 4 can be suppressed, so the collection efficiency is improved.

包含灰塵而向集塵極4流動之離子風之一部分穿過集塵極4之間。由於離子風朝向一方向,故不會互相干涉。Part of the ion wind that contains dust and flows toward the dust collecting pole 4 passes between the dust collecting poles 4. Since the ion wind is oriented in one direction, it will not interfere with each other.

另一方面,與突起部5a之相反側之相反側集塵極4b間,如使用圖6B所說明,藉由使放電極5自中央位置CL偏移,而可使相反側集塵極4b附近之電場強度E2max較無偏移時增加。藉此,突起部5a之相反側之相反側集塵極4b亦藉由庫侖力而有效地進行集塵。即,可藉由離子風有效地捕集繞行至集塵極4之背面即相反側集塵極4b之未捕集之灰塵。On the other hand, between the dust collecting electrode 4b on the opposite side to the opposite side of the protrusion 5a, as explained using FIG. 6B, by displacing the discharge electrode 5 from the center position CL, the vicinity of the dust collecting electrode 4b on the opposite side can be made The electric field strength E2max increases compared with no offset. Thereby, the dust collecting pole 4b on the opposite side to the opposite side of the protrusion 5a also efficiently collects dust by the Coulomb force. That is, the uncollected dust that bypasses the dust collecting electrode 4b on the back side of the dust collecting electrode 4, that is, the back side of the dust collecting electrode 4, can be efficiently collected by the ion wind.

集塵極4所捕集之灰塵藉由捶打而被剝離回收。或者,亦可採用使集塵極移動,並以刷子刮落灰塵之方式、或濕式洗淨。The dust collected by the dust collecting pole 4 is stripped and recovered by thrashing. Alternatively, the dust collector can be moved and wiped off with a brush or wet cleaning.

根據本實施形態,可發揮以下之作用效果。 由於放電極5之本體部5b之中心位於較放電側集塵極4a與相反側集塵極4b間之中央位置CL更遠離放電側集塵極4a之方向,故放電極5之本體部5b與相反側集塵極4b靠近。藉此,可增加放電極5之本體部5b與相反側集塵極4b間之電場強度,且於相反側電極4b中亦可藉由庫侖力而提高集塵效率。According to this embodiment, the following effects can be exerted. Since the center of the body portion 5b of the discharge electrode 5 is located further away from the direction of the discharge side dust collecting electrode 4a than the center position CL between the discharge side dust collecting electrode 4a and the opposite side dust collecting electrode 4b, the body portion 5b of the discharge electrode 5 and The dust collecting pole 4b on the opposite side approaches. Thereby, the electric field strength between the body portion 5b of the discharge electrode 5 and the opposite side dust collecting electrode 4b can be increased, and the dust collecting efficiency can also be improved by the Coulomb force in the opposite side electrode 4b.

另,上述實施形態中,作為放電極5之構成,設為對具有圓形橫剖面之本體部5b設置突起部5a之構成,但如圖7A所示,亦可設為於橫剖面為矩形之角棒5b'設置突起部5a之構成。或如圖7B所示,亦可為穿通平板而形成,且突起部5a與本體部5b''一體構成者。In addition, in the above-mentioned embodiment, as the configuration of the discharge electrode 5, the protrusion 5a is provided to the body portion 5b having a circular cross section, but as shown in FIG. 7A, it may also be configured to have a rectangular cross section The corner bar 5b' is provided with a protrusion 5a. Alternatively, as shown in FIG. 7B, it may be formed through a flat plate, and the protrusion 5a and the body 5b'' are integrally formed.

又,如圖8A及圖8B所示,亦可取代作為上述圓形導管之集塵極4,而採用於平板上形成多個孔之衝孔金屬般之平板狀集塵極4'。或,如圖9A及圖9B所示,亦可採用使形成有多個孔之衝孔金屬般之平板沿氣流G方向交替並規則地折返之彎折板狀集塵極4''。該情形時,放電極5之突起部5a根據對向之彎折板之凹凸而偏移。Moreover, as shown in FIGS. 8A and 8B, instead of the dust collecting electrode 4 as the above-mentioned circular duct, a flat metal dust collecting electrode 4'like a punching metal in which a plurality of holes are formed in a flat plate may be used. Or, as shown in FIGS. 9A and 9B, a bent plate-shaped dust collecting electrode 4'' which alternately and regularly folds back a metal-like flat plate formed with a plurality of holes in the direction of the air flow G may be used. In this case, the protrusion 5a of the discharge electrode 5 is shifted according to the unevenness of the oppositely bent plate.

再者,集塵極4亦可為使金屬製線材沿縱向及橫向等交叉之編織金屬網(例如鎖定壓接編織金屬網等)。由於編織金屬網具有一定開口率,且表面無邊緣,故可同樣地提高集塵極4附近之電場強度。另,金屬網不限於編織金屬網,亦可為如熔接金屬網般使剖面圓形狀線材沿縱向與橫向排列並連接者。In addition, the dust collecting electrode 4 may also be a braided metal mesh (for example, a lock crimped braided metal mesh, etc.) in which metal wires are crossed in the longitudinal direction and the transverse direction. Since the braided metal mesh has a certain aperture ratio and the surface has no edges, the electric field intensity near the dust collecting electrode 4 can be similarly increased. In addition, the metal mesh is not limited to the woven metal mesh, but may also be a wire cross-sectionally arranged and connected in a longitudinal direction and a lateral direction like a welded metal mesh.

電集塵裝置1於空氣淨化用時作為空氣洗淨機使用之情形,粒子滯留於裝置內之時間較短,粒子濃度較低。另一方面,火力發電設備所使用之電集塵裝置1與空氣淨化用時使用之情形不同,規模較大,粒子滯留之時間較長,粒子濃度亦較高。空氣淨化用電集塵裝置1中,若使低濃度粒子以較短之滯留時間通過,則無法以藉由來自放電極5之突起部5a之離子風產生之氣體循環之效果,將粒子捕集至集塵極4。When the electric dust collector 1 is used as an air washer during air purification, the particles stay in the device for a short time and the particle concentration is low. On the other hand, the electric dust collector 1 used in thermal power generation equipment is different from the one used for air purification. It has a larger scale, a longer particle retention time, and a higher particle concentration. In the electric dust collector 1 for air purification, if low-concentration particles are passed through with a short residence time, the particles cannot be captured by the effect of the gas circulation generated by the ion wind from the protrusion 5a of the discharge electrode 5 To dust collector 4.

因此,如圖12所示,較佳於相反側集塵極4b與放電極5間之氣流G之上游側,設置氣體切斷板6。藉由利用氣體切斷板6阻礙氣流G,可降低流動於相反側集塵極4b與放電極5間之氣流之流量,延長穿通集塵極4之粒子之滯留時間,提高捕集性能。Therefore, as shown in FIG. 12, it is preferable to provide the gas cutoff plate 6 on the upstream side of the air flow G between the dust collecting electrode 4 b on the opposite side and the discharge electrode 5. By blocking the airflow G with the gas cutting plate 6, the flow rate of the airflow flowing between the dust collecting electrode 4b on the opposite side and the discharge electrode 5 can be reduced, the retention time of the particles passing through the dust collecting electrode 4 can be extended, and the collection performance can be improved.

1:電集塵裝置 2D:間隔 4:集塵極 4':平板狀集塵極 4'':彎折板狀集塵極 4a:放電側集塵極 4b:相反側集塵極 5:放電極 5a:突起部(電暈放電部) 5b:本體部 5b':角棒 5b'':本體部 5c:安裝框 6:氣體切斷板 A1、A2面積 C1:(放電極之本體部之)中心 C2:中心 C3:中心 CL:中央位置 D1:距離 D2:距離 Dc:直徑 Dd:直徑 E1ave.:平均電場強度 E1max:電場強度 E2ave.:平均電場強度 E2max:電場強度 G:氣流 f:集塵面積 L1:距離 L2:距離 Lb:突起長度 Le:偏移量 Pc:間隔 Pd:間隔 Vn:施加線壓 Vo:施加電壓 w:集塵性指數 x:方向 y:方向 z:方向 η:集塵效率1: Electric dust collector 2D: interval 4: dust collector 4': Flat dust collector 4'': Bending plate-shaped dust collector 4a: Dust collector on the discharge side 4b: Dust collector on opposite side 5: discharge electrode 5a: Protruding part (corona discharge part) 5b: Body part 5b': corner stick 5b'': Body part 5c: Installation frame 6: Gas cut-off board A1, A2 area C1: (of the body of the discharge electrode) center C2: Center C3: Center CL: Central location D1: distance D2: distance Dc: diameter Dd: diameter E1ave.: Average electric field strength E1max: electric field strength E2ave.: average electric field strength E2max: electric field strength G: Airflow f: dust collection area L1: distance L2: distance Lb: protrusion length Le: offset Pc: interval Pd: interval Vn: apply line pressure Vo: applied voltage w: dust collection index x: direction y: direction z: direction η: dust collection efficiency

圖1係顯示本發明之一實施形態之電集塵裝置之立體圖。 圖2係自上方觀察圖1之電集塵裝置之俯視圖。 圖3係自氣流方向觀察圖1之電集塵裝置之前視圖。 圖4A係顯示集塵極與放電極之位置關係之俯視圖。 圖4B係相當於放電極之突起部之高度位置之橫剖視圖。 圖5A係顯示無偏移之情形之放電側放電極與集塵極間之電場強度之圖。 圖5B係顯示無偏移之情形之相反側放電極與集塵極間之電場強度之圖。 圖6A係顯示有偏移之情形之放電側放電極與集塵極間之電場強度之圖。 圖6B係顯示有偏移之情形之相反側放電極與集塵極間之電場強度之圖。 圖7A係顯示放電極之變化例之前視圖。 圖7B係顯示放電極之其他變化例之前視圖。 圖8A係顯示集塵極之變化例之俯視圖。 圖8B係顯示集塵極之變化例之前視圖。 圖9A係顯示集塵極之其他變化例之俯視圖。 圖9B係顯示集塵極之其他變化例之前視圖。 圖10係顯示集塵性能指數比與偏移比之關係之圖表。 圖11係顯示集塵極附近之電場強度與偏移比之關係之圖表。 圖12係顯示本發明之一實施形態之電集塵裝置之俯視圖。FIG. 1 is a perspective view showing an electric dust collector according to an embodiment of the present invention. FIG. 2 is a plan view of the electric dust collector of FIG. 1 viewed from above. FIG. 3 is a front view of the electric dust collector of FIG. 1 viewed from the air flow direction. 4A is a plan view showing the positional relationship between the dust collecting electrode and the discharge electrode. 4B is a cross-sectional view corresponding to the height position of the protrusion of the discharge electrode. FIG. 5A is a graph showing the electric field strength between the discharge side discharge electrode and the dust collecting electrode without deviation. FIG. 5B is a graph showing the electric field strength between the discharge electrode and the dust collecting electrode on the opposite side in the case of no offset. 6A is a graph showing the electric field strength between the discharge side discharge electrode and the dust collecting electrode in the case of deviation. 6B is a graph showing the electric field intensity between the discharge electrode and the dust collecting electrode on the opposite side in the case of deviation. 7A is a front view showing a variation of the discharge electrode. FIG. 7B is a front view showing another modification of the discharge electrode. FIG. 8A is a plan view showing a variation of the dust collecting pole. FIG. 8B is a front view showing a variation of the dust collecting pole. Fig. 9A is a plan view showing another variation of the dust collecting electrode. FIG. 9B is a front view showing other modified examples of the dust collecting pole. Fig. 10 is a graph showing the relationship between the dust collection performance index ratio and the offset ratio. Fig. 11 is a graph showing the relationship between the electric field intensity near the dust collecting pole and the offset ratio. 12 is a plan view showing an electric dust collector according to an embodiment of the present invention.

4:集塵極 4: dust collector

4a:放電側集塵極 4a: Dust collector on the discharge side

4b:相反側集塵極 4b: Dust collector on opposite side

5:放電極 5: discharge electrode

5a:突起部(電暈放電部) 5a: Protruding part (corona discharge part)

5b:本體部 5b: Body part

5c:安裝框 5c: Installation frame

C1:(放電極之本體部之)中心 C1: (of the body of the discharge electrode) center

C2:中心 C2: Center

C3:中心 C3: Center

CL:中央位置 CL: Central location

D1:距離 D1: distance

D2:距離 D2: distance

G:氣流 G: Airflow

x:方向 x: direction

y:方向 y: direction

Claims (5)

一種電集塵裝置,其具備: 放電極,其具有本體部及自該本體部突出之電暈放電用之電暈放電部; 放電側集塵極,其位於上述電暈放電部側;及 相反側集塵極,其隔著上述放電極位於上述放電側集塵極之相反側;且 上述放電極之上述本體部之中心位於較上述放電側集塵極與上述相反側集塵極間之中央位置更靠向遠離上述放電側集塵極之方向。An electric dust collector, including: The discharge electrode has a body part and a corona discharge part for corona discharge protruding from the body part; A dust collecting electrode on the discharge side, which is located on the side of the corona discharge portion; and The dust collector on the opposite side is located on the opposite side of the dust collector on the discharge side through the discharge electrode; and The center of the body portion of the discharge electrode is located further away from the discharge side dust collecting electrode than the center position between the discharge side dust collecting electrode and the opposite side dust collecting electrode. 如請求項1之電集塵裝置,其中 將上述放電極之上述本體部之中心與上述放電側集塵極間之距離設為D1,且將上述放電極之上述本體部之中心與上述相反側集塵極間之距離設為D2之情形時,設為: 1.1≦D1/D2≦2.0。As in the electric dust collector of claim 1, where The distance between the center of the body of the discharge electrode and the discharge side dust collector is D1, and the distance between the center of the body of the discharge electrode and the opposite dust collector is D2 , Set to: 1.1≦D1/D2≦2.0. 如請求項2之電集塵裝置,其中 上述放電側集塵極及上述相反側集塵極分別沿一方向排列; 上述D1為上述放電極之本體部之中心與上述放電側集塵極之排列位置間之距離; 上述D2為上述放電極之本體部之中心與上述相反側集塵極之排列位置間之距離。As in the electric dust collector of claim 2, where The discharge-side dust-collecting pole and the opposite-side dust-collecting pole are arranged in one direction respectively; The D1 is the distance between the center of the body of the discharge electrode and the arrangement position of the discharge side dust collector; The D2 is the distance between the center of the body portion of the discharge electrode and the arrangement position of the dust collector on the opposite side. 如請求項1至3中任一項之電集塵裝置,其中上述放電極與上述放電側集塵極間之電場強度、與上述放電極與上述相反側集塵極間之電場強度相等。The electric dust collector according to any one of claims 1 to 3, wherein the electric field strength between the discharge electrode and the discharge side dust collection electrode is equal to the electric field strength between the discharge electrode and the opposite side dust collection electrode. 如請求項1至3中任一項之電集塵裝置,其中上述電暈放電部之前端位於較上述放電側集塵極與上述相反側集塵極間之上述中央位置更靠向上述相反側集塵極側。The electric dust collector according to any one of claims 1 to 3, wherein the front end of the corona discharge portion is located closer to the opposite side than the center position between the discharge side dust collecting electrode and the opposite side dust collecting electrode Dust collector side.
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