JPH0125623B2 - - Google Patents

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Publication number
JPH0125623B2
JPH0125623B2 JP13406484A JP13406484A JPH0125623B2 JP H0125623 B2 JPH0125623 B2 JP H0125623B2 JP 13406484 A JP13406484 A JP 13406484A JP 13406484 A JP13406484 A JP 13406484A JP H0125623 B2 JPH0125623 B2 JP H0125623B2
Authority
JP
Japan
Prior art keywords
exhaust gas
collector electrode
cleaning
attached
conductive plastic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP13406484A
Other languages
Japanese (ja)
Other versions
JPS6115750A (en
Inventor
Giichi Kikuchi
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.)
KORONA GIKEN KOGYO KK
Original Assignee
KORONA GIKEN KOGYO KK
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 KORONA GIKEN KOGYO KK filed Critical KORONA GIKEN KOGYO KK
Priority to JP59134064A priority Critical patent/JPS6115750A/en
Publication of JPS6115750A publication Critical patent/JPS6115750A/en
Publication of JPH0125623B2 publication Critical patent/JPH0125623B2/ja
Granted legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Electrostatic Separation (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は排ガス浄化装置に関するもので、有害
有臭ガスおよびミストとダストが混在して発生す
る化学工場、金属製練工場、アスフアルトプラン
ト、ニユーセラミツク、食品、製薬工場および電
子部品工場等の各種産業の現場における空調や公
害防止に利用可能である。 従来の技術 従来は排ガス浄化のためには気液接触用の各種
充填物を使用した洗滌装置のみを設置して有害ガ
スを対象に公害防止を行つている。これは有害ガ
スのみならず、ある程度のダストも除去できるこ
とが知られている。しかし気液の接触のみによつ
てダストを捕集するものであるから排ガス洗滌装
置では1μ以下の微粒子の除去は全く不可能であ
り、また気液接触によつて多くのミストが排ガス
中に放出される欠点があり、かかる極数粒子の除
去のためには別途に従来型の大型で高価な電気集
塵機を設置している。 発明が解決しようとする問題点 このように公害発生源となる排ガス浄化のため
に排ガス洗滌塔と電気集塵機とを別々に設置する
ことは、スペース、価格の点においても無駄が多
い。本発明は排ガス洗滌塔と電気集塵機を一体構
造とすることによりかかる無駄を排除することを
目的とするものである。 かかる目的のもとに提案された特公昭56−
29585号の排煙浄化装置がある。これはガスが流
通する直立浄化装置の上部に平板式の電気集塵
部、下部にガス洗滌部を設置したものであるが、
平板式であるために電気集塵部の静電気凝集作用
が水滴により電界強度の不整による火花放電発生
のため不充分であり、また特公昭57−45620号の
ごとく湿式電気集塵装置において平板の集塵極を
使用すると集塵極間を40cm以上離す必要が生じて
装置が大型となる。 問題点を解決するための手段 本発明はこれらの点に鑑み、直立浄化装置の上
部に湿式の電気集塵部、下部にガス洗滌部を設け
該湿式の電気集塵部には平板状でなく導電性のパ
イプを並設してスダレ状に形成した集塵極に傾斜
を附して交互に設置することにより、多数の針状
片が同一方向に植設された放電極の作用と相俟つ
て、前記平板式集塵極を内蔵した装置と比較して
洗滌スプレーによる運転電圧の低下やスパークに
よる性能低下がなく、また2種類(水と薬液)の
洗滌液を同時に使用することが可能となり、した
がつて高電圧、高電流密度、高効率な小型かつ安
価な排ガス浄化装置を提供するものである。 作 用 本発明は通常の洗滌塔において除去不可能とさ
れている10μ以下の微粒子を、スダレ状に形成
し、傾斜を附した集塵極と多数の針状片が同一方
向に植設された放電極を当該洗滌塔の上部に内蔵
することにより除去するものであつて、その結
果、従来の排ガス洗滌装置に多く見られる1μ以
下の極微粒子による白煙およびミストの処理に特
に有効である。なお、スダレ状集塵極に付着する
ミストを本装置外被側に分離しやすく、しかも水
滴による電界強度の不整による火花放電発生を抑
制するため、ガス流れ方向に対して5度以上傾斜
させてスダレ状集塵極を配置している。 実施例 第1図は本発明実施の第1例を示し、直立浄化
装置の本体1の下部に多孔板2を内蔵しその上部
に下部洗滌用スプレー3を取附けてガス入口4か
ら導入される有害有臭ガスを除去し、さらにその
上部に中空金属棒または導電性プラスチツクパイ
プをガス流れ方向に対してスダレ状にかつθ(5
度以上)の傾斜角度を附して設置した集塵極5
と、断面円筒形の金属棒または導電性プラスチツ
ク棒に多数の針状片が同一方向に植設された放電
極6とを配置し、さらに上方に上部洗滌用スプレ
ー7を設けたもので、8は高圧電源装置、9は排
水口である。なお、同図Dに示すものは放電極6
の変形例で、針状片の植設方向がガス流れと平行
のものである。 第2図は本発明の実施第2例を示すもので、実
施第1例と異なる点は多孔板に代り充填物10を
内蔵するものである。またCは充填物10の形状
の2、3の例を示し、この外にも各種形状のもの
が使用できるが、ロおよびハに示すものは比表面
積が75m2/m3以上の捕集表面を有するものである。 第3図は放電極の各種形状を示し、イは丸線、
ロは星型線、ハは角線、ニは角捻り線、ホはバー
ブドワイヤー、ヘは丸棒突起型、トはアングル突
起型であつて、第1および第2実施例においては
上記への丸棒突起型が使用されている。 第4図は各種集塵極の形状を示すもので、イは
ロツドカーテン型、ロはポケツト型、ハはフイン
プレート型、ニはジグザグ型、ホは本発明実施例
におけるスダレ型、ヘはフインプレート型U、ト
は角波型、チは溝型、リは二重板型、ヌはナス型
である。 発明の効果 本発明によるとスダレ状に配置した集電極をガ
ス流れと平行で水平方向に対して5度以上傾斜さ
せているので洗浄液が直下に落下せず側壁に回収
することがきるので、2種類(水と薬液)の洗浄
液を同時に使用することができて洗浄能力が倍増
する上に、多数の針状片が同一方向に植設された
放電極の作用と相俟つて従来の平板式集塵極を内
蔵した装置と比較して著しい高電圧、高電流密
度、高効率が可能となる。 本発明による排ガス浄化装置の効果の1例は次
の通りである。 入口排ガス濃度 288PPM 入口ダスト濃度 105mg/Nm3 出口排ガス濃度 7PPM 出口ダスト濃度 4mg/Nm3 排ガス除去率 97.5% ダスト除去率 96.2% 本発明による寸法節約は次の通りである。 設計条件 処 理 風 量 9000Nm3/H 入口排ガス濃度 270PPM 入口ダスト濃度 55mg/Nm3 出口排ガス濃度 10PPM 出口ダスト濃度 5mg/Nm3 【表】
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to an exhaust gas purification device, and is applicable to chemical factories, metal smelting factories, asphalt plants, new ceramic plants, etc. where harmful odor gases, mist and dust are generated in a mixed manner. It can be used for air conditioning and pollution prevention at various industrial sites such as food, pharmaceutical factories, and electronic component factories. Conventional Technology Conventionally, in order to purify exhaust gas, only a cleaning device using various gas-liquid contact fillers has been installed to prevent pollution by targeting harmful gases. It is known that this method can remove not only harmful gases but also a certain amount of dust. However, since dust is collected only through gas-liquid contact, it is completely impossible for exhaust gas cleaning equipment to remove particles smaller than 1μ, and a large amount of mist is released into the exhaust gas due to gas-liquid contact. However, in order to remove such particles, a conventional large and expensive electrostatic precipitator is installed separately. Problems to be Solved by the Invention Installing an exhaust gas scrubbing tower and an electrostatic precipitator separately for purifying exhaust gas, which is a source of pollution, is wasteful in terms of space and cost. The present invention aims to eliminate such waste by integrating the exhaust gas scrubbing tower and the electrostatic precipitator into an integrated structure. A special public service proposed for this purpose in 1972-
There is an exhaust gas purification device No. 29585. This is an upright purification device through which gas flows, with a flat plate electrostatic precipitator installed at the top and a gas cleaning unit at the bottom.
Because it is a flat plate type electrostatic precipitator, the electrostatic agglomeration effect of the electrostatic precipitator is insufficient due to the generation of spark discharge due to uneven electric field strength due to water droplets. If dust electrodes are used, it is necessary to space the dust collecting electrodes at least 40 cm apart, which increases the size of the device. Means for Solving the Problems In view of these points, the present invention provides a wet electrostatic precipitator in the upper part of an upright purification device and a gas cleaning part in the lower part, and the wet electrostatic precipitator has a non-flat plate shape. By arranging conductive pipes in parallel to form a sag-like dust collection electrode and installing them alternately at an angle, this works in conjunction with the action of a discharge electrode with a large number of needle-like pieces planted in the same direction. As a result, compared to the device with a built-in flat plate type dust collecting electrode, there is no drop in operating voltage due to cleaning spray or performance degradation due to sparks, and it is also possible to use two types of cleaning liquid (water and chemical) at the same time. Therefore, a compact and inexpensive exhaust gas purification device with high voltage, high current density, and high efficiency is provided. Function The present invention forms fine particles of 10μ or less, which are said to be impossible to remove in a normal washing tower, into a sagging shape, and has an inclined dust collection electrode and a large number of needle-like pieces planted in the same direction. A discharge electrode is built into the upper part of the scrubbing tower to remove it, and as a result, it is particularly effective in treating white smoke and mist caused by ultrafine particles of 1 μm or less, which are often found in conventional exhaust gas scrubbing equipment. In addition, in order to easily separate the mist adhering to the sagging dust collecting electrode to the outer cover of this device, and to suppress the occurrence of spark discharge due to uneven electric field strength due to water droplets, the electrode is tilted at an angle of 5 degrees or more with respect to the gas flow direction. A sagging dust collection electrode is installed. Embodiment FIG. 1 shows a first embodiment of the present invention, in which a perforated plate 2 is built into the lower part of the main body 1 of an upright purifier, a lower cleaning spray 3 is attached to the upper part, and gas is introduced from the gas inlet 4. After removing the harmful odor gas, a hollow metal rod or conductive plastic pipe is placed above it in a sagging shape with respect to the gas flow direction.
Dust collection pole 5 installed with an inclination angle of
and a discharge electrode 6 in which a large number of needle-shaped pieces are implanted in the same direction on a metal rod or conductive plastic rod with a cylindrical cross section, and an upper cleaning spray 7 is provided above. 9 is a high-voltage power supply, and 9 is a drain port. Note that the one shown in figure D is the discharge electrode 6.
In this modification, the needle-like pieces are installed in a direction parallel to the gas flow. FIG. 2 shows a second embodiment of the present invention, which differs from the first embodiment in that a filler 10 is built in instead of the perforated plate. In addition, C shows a few examples of the shape of the packing 10, and various other shapes can be used, but those shown in B and C have a collection surface with a specific surface area of 75 m 2 /m 3 or more. It has the following. Figure 3 shows various shapes of discharge electrodes, A is a round wire,
B is a star-shaped wire, C is a square wire, D is a square twisted wire, E is a barbed wire, H is a round bar protrusion type, and G is an angled protrusion type. A round bar protrusion type is used. Fig. 4 shows the shapes of various dust collecting electrodes, A is a rod curtain type, B is a pocket type, C is a fin plate type, D is a zigzag type, E is a sagging type in the embodiment of the present invention, and F is a fin plate. Types U and G are square wave type, Chi is groove type, Li is double plate type, and Nu is eggplant type. Effects of the Invention According to the present invention, since the collecting electrode arranged in a sagging shape is parallel to the gas flow and inclined at an angle of 5 degrees or more with respect to the horizontal direction, the cleaning liquid can be collected on the side wall without falling directly below. In addition to being able to use different cleaning solutions (water and chemical solutions) at the same time, which doubles the cleaning capacity, this combination with the action of the discharge electrode, which has many needle-like pieces planted in the same direction, makes it possible to use different types of cleaning solutions (water and chemical solutions) at the same time. Compared to devices with built-in dust electrodes, significantly higher voltages, higher current densities, and higher efficiency are possible. An example of the effects of the exhaust gas purification device according to the present invention is as follows. Inlet exhaust gas concentration 288PPM Inlet dust concentration 105mg/Nm 3Outlet exhaust gas concentration 7PPM Outlet dust concentration 4mg/Nm 3Exhaust gas removal rate 97.5% Dust removal rate 96.2% The size savings by the present invention are as follows. Design condition treatment Air volume 9000Nm 3 /H Inlet exhaust gas concentration 270PPM Inlet dust concentration 55mg/Nm 3 outlet exhaust gas concentration 10PPM Outlet dust concentration 5mg/Nm 3 [Table]

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

第1図A,B,C,Dは本発明実施の第1例を
示す正面断面図、側面断面図、要部平面図および
要部変形例、第2図A,B,C,Dは本発明実施
の第2例を示す正面断面図、側面断面図、要部斜
視図および要部変形例、第3図は各種放電極の説
明図、第4図は各種集塵極の説明図である。 図中の符号はそれぞれ下記部材を示す。1…本
体、2…多孔板、3…下部洗滌用スプレー、4…
ガス入口、5…集塵極、6…放電極、7…上部洗
滌用スプレー、8…高圧電源装置、9…排水口、
10…充填物。
Figures 1A, B, C, and D are a front sectional view, a side sectional view, a plan view of the main part, and a modified example of the main part, showing a first example of implementing the present invention, and Figures 2A, B, C, and D are the main parts of the present invention. A front sectional view, a side sectional view, a perspective view of the main part, and a modification of the main part showing a second example of carrying out the invention, FIG. 3 is an explanatory diagram of various discharge electrodes, and FIG. 4 is an explanatory diagram of various dust collection electrodes. . The symbols in the drawings indicate the following members, respectively. 1... Main body, 2... Perforated plate, 3... Lower part cleaning spray, 4...
Gas inlet, 5... Dust collection electrode, 6... Discharge electrode, 7... Upper cleaning spray, 8... High voltage power supply, 9... Drain port,
10...Filling.

Claims (1)

【特許請求の範囲】 1 排ガスを下方から上方に導く堅型の本体の下
部に多孔板または洗滌用充填物を内蔵しその上部
に洗滌用スプレーを取附け、さらにその上部に中
空金属棒または導電性プラスチツクパイプをガス
流れ方向に対してスダレ状に設置した集電極とこ
れに対向した金属材または導電性プラスチツク材
よりなる放電極とを配置するとともにその上部に
洗滌用スプレーを取附けたものにおいて、前記放
電極が断面円筒形の金属棒または導電性プラスチ
ツク棒に多数の針状片が同一方向に植設されたも
のであり、かつ前記スダレ状に配置した集電極を
ガス流れと平行で水平方向に対して5度以上傾斜
させたことを特徴とする排ガス浄化装置。 2 前記スダレ状集塵極は集塵極間を40cm以下と
し、従来の湿式電気集塵機より、同一容積に於け
る集塵面積を2倍以上多く取れるようにしたこと
を特徴とする特許請求の範囲第1項に記載の排ガ
ス浄化装置。
[Claims] 1. A perforated plate or cleaning filler is built into the lower part of the rigid body that guides the exhaust gas from below to the upper side, a cleaning spray is attached to the upper part, and a hollow metal rod or conductive material is attached to the upper part of the solid body. A collector electrode made of a conductive plastic pipe installed in a sagging manner with respect to the gas flow direction, and a discharge electrode made of a metal material or a conductive plastic material opposed to the collector electrode are arranged, and a cleaning spray is attached to the upper part of the collector electrode. , the discharge electrode is a metal rod or a conductive plastic rod with a cylindrical cross section and a large number of needle-like pieces planted in the same direction, and the collector electrode arranged in a sagging shape is parallel to the gas flow and horizontal. An exhaust gas purification device characterized by being inclined at an angle of 5 degrees or more with respect to a direction. 2 Claims characterized in that the distance between the dust collection electrodes is 40 cm or less, and the dust collection area in the same volume can be more than twice as large as that of a conventional wet electrostatic precipitator. The exhaust gas purification device according to item 1.
JP59134064A 1984-06-30 1984-06-30 Apparatus for purifying exhaust gas Granted JPS6115750A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59134064A JPS6115750A (en) 1984-06-30 1984-06-30 Apparatus for purifying exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59134064A JPS6115750A (en) 1984-06-30 1984-06-30 Apparatus for purifying exhaust gas

Publications (2)

Publication Number Publication Date
JPS6115750A JPS6115750A (en) 1986-01-23
JPH0125623B2 true JPH0125623B2 (en) 1989-05-18

Family

ID=15119521

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59134064A Granted JPS6115750A (en) 1984-06-30 1984-06-30 Apparatus for purifying exhaust gas

Country Status (1)

Country Link
JP (1) JPS6115750A (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0647065B2 (en) * 1990-11-20 1994-06-22 工業技術院長 Desulfurization and denitration equipment using corona discharge
JP4778960B2 (en) * 2004-05-08 2011-09-21 黄清豹 Dust removal device for fuel oil
US8790444B2 (en) * 2011-03-01 2014-07-29 Rsr Technologies, Inc. Wet electrostatic precipitator and related methods
WO2014123202A1 (en) * 2013-02-07 2014-08-14 三菱重工メカトロシステムズ株式会社 Dust collection apparatus, dust collection system, and dust collection method
WO2015068209A1 (en) * 2013-11-05 2015-05-14 三菱重工メカトロシステムズ株式会社 Dust collection device and dust collection method
CN103949127B (en) * 2014-04-02 2016-01-20 华电电力科学研究院 The embedded wet electrical dust precipitator of flue and electro dust removing method thereof
CN105080712A (en) * 2015-09-18 2015-11-25 广东美的制冷设备有限公司 Electrostatic dust collection device and method
CN106733193A (en) * 2015-11-19 2017-05-31 欧亚科技环保工程有限公司 The battery lead plate of precipitator

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49119274A (en) * 1973-03-20 1974-11-14
JPS521149A (en) * 1975-06-23 1977-01-06 Shimadzu Corp Method of knotting wivers thread

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5119081U (en) * 1975-07-10 1976-02-12

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49119274A (en) * 1973-03-20 1974-11-14
JPS521149A (en) * 1975-06-23 1977-01-06 Shimadzu Corp Method of knotting wivers thread

Also Published As

Publication number Publication date
JPS6115750A (en) 1986-01-23

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