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JP6167326B2 - Paint mist processing equipment - Google Patents
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JP6167326B2 - Paint mist processing equipment - Google Patents

Paint mist processing equipment Download PDF

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JP6167326B2
JP6167326B2 JP2013051342A JP2013051342A JP6167326B2 JP 6167326 B2 JP6167326 B2 JP 6167326B2 JP 2013051342 A JP2013051342 A JP 2013051342A JP 2013051342 A JP2013051342 A JP 2013051342A JP 6167326 B2 JP6167326 B2 JP 6167326B2
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porous filter
mist
air
coating
processing apparatus
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JP2014176789A (en
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加藤 亮
亮 加藤
加藤 務
務 加藤
田代 義和
義和 田代
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Panasonic Intellectual Property Management Co Ltd
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Description

本発明は、塗装ブースで発生する塗装ミストを捕集して空気を清浄化する塗装ミスト処理装置に関するものである。   The present invention relates to a paint mist processing apparatus that collects paint mist generated in a paint booth and cleans the air.

従来の塗装ブースの空気を清浄化して外に排気する装置として、図10に示すような水滴を噴霧して塗装ミストを取り込み、その水滴を仕切り板で空気から分離する湿式処理装置が知られている。   As a conventional apparatus for purifying the air of a paint booth and exhausting it outside, a wet processing apparatus is known which sprays water droplets as shown in FIG. 10 to take in paint mist and separates the water droplets from the air with a partition plate. Yes.

以下、その湿式処理装置について図10を参照しながら説明する。   Hereinafter, the wet processing apparatus will be described with reference to FIG.

図10に示すように塗装ブース101では塗装ロボット102から例えば有機溶剤を溶媒とした塗料がスプレーされているため、有機溶剤を含む塗装ミスト103が充満している。塗装対象物104への塗装品質を確保するために塗装ミスト103を含む空気は排気ファン105によって外に排出されるが、そのまま排出すると外の環境が塗装ミスト103よって大きく汚染されてしまうため、塗装ブース101と排気ファン105の間に湿式処理装置106が設置されている。   As shown in FIG. 10, in the painting booth 101, for example, a paint using an organic solvent as a solvent is sprayed from the painting robot 102, so that the painting mist 103 containing the organic solvent is filled. The air containing the coating mist 103 is discharged outside by the exhaust fan 105 in order to ensure the coating quality on the object 104 to be coated. However, if the air is discharged as it is, the outside environment will be greatly contaminated by the coating mist 103. A wet processing apparatus 106 is installed between the booth 101 and the exhaust fan 105.

湿式処理装置106は水滴噴霧器107によって水滴108を接触室109に散布して水滴108に塗装ミスト103を取り込み、接触室109の風下に設けられた仕切り板110によって水滴108を空気から分離する。このような原理で空気中の塗装ミスト103を捕集する。捕集された塗装ミスト103を含む水滴108は仕切り板110から滴り落ちて水受け槽111に回収される。水受け槽111の中には泥状のスラッジ112が溜まる。これは有機溶剤を含む半液体状の塗装ミスト103が水の中でくっつきあうためである。スラッジ112は脱水処理され、残ったスラッジ塊は焼却処理される。   The wet processing apparatus 106 sprays water droplets 108 into the contact chamber 109 by the water droplet sprayer 107 to take the coating mist 103 into the water droplets 108, and separates the water droplets 108 from the air by the partition plate 110 provided leeward of the contact chamber 109. The paint mist 103 in the air is collected based on such a principle. The water droplets 108 including the collected paint mist 103 are dropped from the partition plate 110 and collected in the water receiving tank 111. Mud sludge 112 accumulates in the water receiving tank 111. This is because the semi-liquid coating mist 103 containing an organic solvent adheres in water. The sludge 112 is dewatered and the remaining sludge mass is incinerated.

このような従来の湿式処理装置は塗装ミストの捕集に使う水によって処理空気の湿度が上がってしまう。塗装品質は湿度に大きく影響するため処理した空気は全て外へ排気しなくてはならず、塗装ブースの空調コストが大きく嵩むという課題を有する。   In such a conventional wet processing apparatus, the humidity of the processing air is increased by the water used for collecting the coating mist. Since the coating quality greatly affects the humidity, all the processed air must be exhausted to the outside, and the air conditioning cost of the coating booth is greatly increased.

この課題を解決するには、図11に示すような水滴108を噴霧しない乾式のミスト処理装置を使うという方法がある(塗装ミストではなく油ミスト処理装置であるが、例えば、特許文献1参照)。   In order to solve this problem, there is a method of using a dry mist processing apparatus that does not spray water droplets 108 as shown in FIG. 11 (this is an oil mist processing apparatus instead of a paint mist, but see, for example, Patent Document 1). .

以下、その油ミスト処理装置について説明する。図11に示す油ミスト処理装置は第1の多孔スクリーン113と第2の多孔スクリーン114とが相互に180度反転して配置され、その下流側に濾過フィルタ115が設けられた構成となっている。これにより第1の多孔スクリーン113の開口A117は油ミスト含有気体の流れ方向116に対して角度αをもって斜めに開口し、第2の多孔スクリーン114の開口B118は反対に−αをもって斜めに開口している。油ミスト含有気体は流れ方向116に沿って先ず第1の多孔スクリーン113において下降流119となり、つづいて第2の多孔スクリーン114においては反転して上昇流120となる。油ミスト含有気体に含まれる油ミスト及び油蒸気等の油分は油含有気体の反転に於ける慣性および同油含有気体の多孔スクリーン壁面への衝突により除去される。またこれら多孔スクリーン113、114で除去されなかった微細な粒子は濾過フィルタ115により除去される。   Hereinafter, the oil mist processing apparatus will be described. The oil mist treatment apparatus shown in FIG. 11 has a configuration in which a first perforated screen 113 and a second perforated screen 114 are arranged so as to be inverted by 180 degrees and a filter filter 115 is provided on the downstream side thereof. . As a result, the opening A117 of the first perforated screen 113 opens obliquely with an angle α with respect to the flow direction 116 of the oil mist-containing gas, and the opening B118 of the second perforated screen 114 opens obliquely with −α. ing. The oil mist-containing gas first becomes a downward flow 119 in the first perforated screen 113 along the flow direction 116, and then reverses into the upward flow 120 in the second perforated screen 114. Oil components such as oil mist and oil vapor contained in the oil mist-containing gas are removed by inertia in the reversal of the oil-containing gas and collision of the oil-containing gas with the perforated screen wall surface. Further, fine particles that are not removed by the perforated screens 113 and 114 are removed by the filtration filter 115.

特開平8−117537号公報(第5頁、図2)JP-A-8-117537 (5th page, FIG. 2)

従来の湿式処理装置では処理空気が加湿されるため塗装ブースに戻して空調費を削減することができない。また、特許文献1による油ミスト処理装置では多孔スクリーンで除去されなかった油ミストが濾過フィルタを目詰まらせ、処理空気が流れなくなって油ミストを捕集できなくなるという課題があった。   In the conventional wet processing apparatus, since the processing air is humidified, it is not possible to return to the painting booth to reduce the air conditioning cost. Moreover, in the oil mist processing apparatus by patent document 1, the oil mist which was not removed with the perforated screen clogged the filtration filter, and there existed a subject that processing air stopped flowing and oil mist could not be collected.

そこで本発明は、上記従来の課題を解決するものであり、加湿および目詰まりをさせずに高い捕集効率で塗装ミストを捕集し続ける塗装ミスト処理装置を提供することを目的とする。   SUMMARY OF THE INVENTION The present invention solves the above-described conventional problems, and an object of the present invention is to provide a paint mist processing apparatus that continues to collect paint mist with high collection efficiency without humidification and clogging.

上記課題を解決するために、本発明の塗装ミスト処理装置は、塗装ブースから排出された塗装ミストを含んだ空気を処理して前記塗装ブースに戻す通風経路内に設置される塗装ミスト処理装置であってともに空気が通過できる多孔質板状の金属もしくはセラミックスからなる、通風方向から見て異なる位置にスリットを有する多孔質フィルタAおよび多孔質フィルタBとを通風方向に一定の間隔を設けながら交互に積層し、前記スリットの壁に通風方向上流側から下流側に向けてはみ出した整流板を設けたことにより初期の目的を達成するものである。 In order to solve the above problems, paint mist processing apparatus of the present invention is a paint mist processing unit that will be installed in the process the air containing the discharged paint mist from paint booth ventilation path back to the painting booth The porous filter A and the porous filter B, both of which are made of porous plate-like metal or ceramics through which air can pass and have slits at different positions when viewed from the ventilation direction, are provided with a certain interval in the ventilation direction. The initial object is achieved by providing the current plates that are alternately stacked and protrude from the upstream side toward the downstream side in the ventilation direction on the wall of the slit .

本発明の塗装ミスト処理装置は、多孔質フィルタAおよび多孔質フィルタBが作るジグザグの通風路だけでなく、多孔質フィルタAおよび多孔質フィルタBの中をも処理空気が通過するため、ジグザグの通風路を通過する際に得られる慣性作用と多孔質フィルタAおよび多孔質フィルタBが有する濾過作用の2つの作用が塗装ミストに働くことになり、高い捕集効率が得られる。また、処理空気が中を通過できないただの板を積層した場合と比べて処理空気を通過させる時に発生する圧力損失を低減することができる。また、多孔質フィルタAおよび多孔質フィルタBが塗装ミストによって目詰まりしても処理空気を通過させるためのジグザグの通風路は確保されており、目詰まりによって処理空気が流れなくなることはなく、引き続き塗装ミストを捕集処理することができる。
特に、前記スリットの壁に通風方向上流側から下流側に向けてはみ出した整流板を設けたことにより、圧力損失の増大を防ぐとともに塗装ミストの慣性作用による衝突効果を得ることができ高い捕集効率が得られる。
In the coating mist processing apparatus of the present invention, the processing air passes not only in the zigzag ventilation path created by the porous filter A and the porous filter B but also in the porous filter A and the porous filter B. Two actions of the inertia action obtained when passing through the ventilation path and the filtration action of the porous filter A and the porous filter B act on the coating mist, and a high collection efficiency is obtained. Moreover, the pressure loss which generate | occur | produces when letting process air pass can be reduced compared with the case where only the board which process air cannot pass through is laminated | stacked. Further, even if the porous filter A and the porous filter B are clogged by the coating mist, a zigzag ventilation path for allowing the processing air to pass therethrough is secured, and the clogging does not stop the processing air from flowing. Paint mist can be collected.
In particular, by providing a baffle plate that protrudes from the upstream side to the downstream side in the ventilation direction on the wall of the slit, it is possible to prevent an increase in pressure loss and to obtain a collision effect due to the inertial action of the paint mist. Efficiency is obtained.

本発明の実施の形態の塗装ミスト処理装置の上面を示す構成図The block diagram which shows the upper surface of the coating mist processing apparatus of embodiment of this invention 同通風方向から見た多孔質フィルタの顕微鏡写真Photomicrograph of a porous filter viewed from the same ventilation direction 同スリットをフランジ構造にした塗装ミスト処理装置の上面を示す構成図The block diagram which shows the upper surface of the paint mist processing equipment which made the slit into the flange structure 同複数のスリットを設けた塗装ミスト処理装置を斜めから見た図A view of the paint mist processing equipment with multiple slits seen from an angle 同塗装ミスト処理装置を導入した塗装ブースを示す図A figure showing the painting booth that introduced the painting mist processing equipment 同多孔質フィルタが下流側から順に手前に引き出されて再生される図The same porous filter is pulled out from the downstream side in order and regenerated. 同多孔質フィルタが下流側から順に奥に引き出されて再生される図The same porous filter is pulled out from the downstream side in order and regenerated 本発明の実施例1の比較ユニットを示す構成図The block diagram which shows the comparison unit of Example 1 of this invention 同実施ユニットおよび比較ユニットの塗装ミスト捕集効率と圧力損失のグラフGraph of paint mist collection efficiency and pressure loss of the same unit and comparison unit 従来の湿式処理装置を示す構成図Configuration diagram showing conventional wet processing equipment 特許文献1記載の油ミスト処理装置を示す構成図The block diagram which shows the oil mist processing apparatus of patent document 1

以下、本実施の形態について図面を参照しながら説明する。   Hereinafter, the present embodiment will be described with reference to the drawings.

(実施の形態)
塗装ミスト処理装置の上面を示す構成図を図1に、通風方向から見た多孔質フィルタの顕微鏡写真を図2に、スリットをフランジ構造にした塗装ミスト処理装置の上面を示す構成図を図3に、複数のスリットを設けた塗装ミスト処理装置を斜めから見た図を図4に、同塗装ミスト処理装置を導入した塗装ブースを示す図を図5に、多孔質フィルタが下流側から順に手前側に引き出されて再生される図を図6に、多孔質フィルタが下流側から順に奥側に引き出されて再生される図を図7に示す。
(Embodiment)
FIG. 1 is a configuration diagram showing the upper surface of the coating mist processing apparatus, FIG. 2 is a micrograph of the porous filter viewed from the ventilation direction, and FIG. 3 is a configuration diagram showing the upper surface of the coating mist processing apparatus having a slit flange structure. Fig. 4 is a perspective view of a coating mist processing apparatus provided with a plurality of slits, Fig. 5 is a diagram showing a coating booth in which the coating mist processing apparatus is introduced, and the porous filter is in front of the downstream side. FIG. 6 shows a drawing that is pulled out and regenerated, and FIG. 7 shows a drawing that the porous filter is drawn and regenerated in order from the downstream side.

図1に示すように本発明の塗装ミスト処理装置9は中央にスリット10を有する多孔質フィルタAa1、Ab3、Ac5、Ad7と、両端にスリット10を有する多孔質フィルタBa2、Bb4、Bc6、Bd8からなり、上流側から順に多孔質フィルタAa1、Ba2、Ab3、Bb4、Ac5、Bc6、Ad7、Bd8の順で一定の間隔を設けながら積層した構造を有する。   As shown in FIG. 1, the coating mist processing apparatus 9 of the present invention comprises a porous filter Aa1, Ab3, Ac5, Ad7 having a slit 10 at the center and porous filters Ba2, Bb4, Bc6, Bd8 having slits 10 at both ends. It has a structure in which porous filters Aa1, Ba2, Ab3, Bb4, Ac5, Bc6, Ad7, and Bd8 are stacked in this order from the upstream side while providing a constant interval.

各々の多孔質フィルタは図2に示すように多数の孔27を有しており、例えば、多孔質フィルタAa1およびBa2は厚さ5〜15mm、孔径3〜4mm、多孔質フィルタAb3およびBb4は厚さ5〜15mm、孔径2〜3mm、多孔質フィルタAc5およびBc6は厚さ5〜15mm、孔径1〜2mm、多孔質フィルタAd7およびBd8は厚さ5〜15mm、孔径0.5〜1mmとなっており、下流側になるほど多孔質フィルタの孔径が小さくなっている。   Each porous filter has a large number of holes 27 as shown in FIG. 2. For example, the porous filters Aa1 and Ba2 have a thickness of 5 to 15 mm, the pore diameters 3 to 4 mm, and the porous filters Ab3 and Bb4 have a thickness. 5 to 15 mm, pore diameters 2 to 3 mm, porous filters Ac5 and Bc6 are 5 to 15 mm thick, pore diameters 1 to 2 mm, porous filters Ad7 and Bd8 are 5 to 15 mm thick, and pore diameters 0.5 to 1 mm In addition, the pore diameter of the porous filter becomes smaller toward the downstream side.

また、これら多孔質フィルタは金属もしくはセラミックスからなり、処理空気を通過させても撓ままないため処理空気の通風路を常に確保できる。また、撓まないため高圧洗浄水を当てて塗装ミストを楽に剥がすことができ、また、自己燃焼しないため600℃程度に加熱して塗装ミストを燃焼除去することも可能である。   In addition, these porous filters are made of metal or ceramics and do not remain bent even when the processing air is passed through, so that a ventilation path for the processing air can always be secured. Moreover, since it does not bend, the coating mist can be easily peeled off by applying high-pressure washing water, and since it does not self-combust, it can be heated to about 600 ° C. to burn off the coating mist.

処理空気は通風方向11に沿って上流側から導入され、下流側から排出される。その際に矢印の空気の流れ12が示すように各々の多孔質フィルタが作るジグザグの通風路を通過すると同時に各々の多孔質フィルタの中をも通過する。ジグザグの通風路が有する急な曲がり角を処理空気が通過する際に、曲がりきれずにまっすぐに行こうとする慣性作用が処理空気中に含まれる塗装ミストに働く。この慣性作用によって塗装ミストは通風路の壁や多孔質フィルタの表面に付着し、処理空気中から除去される。   The processing air is introduced from the upstream side along the ventilation direction 11 and discharged from the downstream side. At that time, as indicated by the air flow 12 indicated by the arrow, the air passes through the zigzag ventilation path formed by each porous filter and simultaneously passes through each porous filter. When the processing air passes through the steep corners of the zigzag ventilation path, an inertial action that tries to go straight without being bent acts on the coating mist contained in the processing air. By this inertial action, the coating mist adheres to the walls of the ventilation path and the surface of the porous filter and is removed from the processing air.

また、図2に示すように多孔質フィルタは多孔性であり、一部の処理空気はジグザグの通風路を通らずに多孔質フィルタの中を通過する。その際に多孔質フィルタの濾過作用によって処理空気中の塗装ミストは捕集される。   Further, as shown in FIG. 2, the porous filter is porous, and a part of the processing air passes through the porous filter without passing through the zigzag ventilation path. At that time, the coating mist in the processing air is collected by the filtering action of the porous filter.

この濾過作用は多孔質フィルタが目詰まりするまで継続して働き続け、その間はジグザグの通風路を通過する際の慣性作用と多孔質フィルタを通過する際の濾過作用の二つが塗装ミストに働くことによって高い捕集効率が得られる。   This filtering action continues to work until the porous filter is clogged, and during that time, the inertia action when passing through the zigzag ventilation path and the filtering action when passing through the porous filter act on the paint mist. High collection efficiency can be obtained.

また、多孔質フィルタが目詰まりするまでの間は低い圧力損失が得られる。目詰まりして多孔質フィルタの中を処理空気が通過しなくなった後もジグザグの通風路は確保されているため処理空気は塗装ミスト処理装置9の中を流れ続け、一定以上の高い捕集効率を得ることができる。   Further, a low pressure loss can be obtained until the porous filter is clogged. Even after clogged and the processing air does not pass through the porous filter, the zigzag ventilation path is secured, so that the processing air continues to flow through the coating mist processing device 9 and has a high collection efficiency above a certain level. Can be obtained.

目詰まりした後に多孔質フィルタに高圧洗浄水を当てる、もしくは多孔質フィルタを加熱して塗装ミストを燃焼するといった方法で塗装ミストを除去し、多孔質フィルタを再生することができ、再生することで高い捕集効率と低い圧力損失を再び得ることができる。   After clogging, the porous filter can be regenerated by applying high pressure washing water to the porous filter or removing the paint mist by heating the porous filter and burning the paint mist. High collection efficiency and low pressure loss can be obtained again.

粒子径の大きい塗装ミストほど慣性作用および濾過作用が大きく働き、除去されやすい。そのため塗装ミスト処理装置9の上流側で粒子径の大きい塗装ミストが除去され、下流側に行くほど粒子径の小さい塗装ミストが除去されずに処理空気中に残る。そこで本発明の塗装ミスト処理装置9のように上流側の多孔質フィルタの孔径を大きくし、下流側になるに従って孔径を小さくすることによって高い捕集効率とより低い圧力損失を得ることができる。   A paint mist having a larger particle diameter has a greater inertial action and filtering action and is more easily removed. Therefore, the coating mist having a large particle diameter is removed on the upstream side of the coating mist processing apparatus 9, and the coating mist having a small particle diameter is not removed and remains in the processing air toward the downstream side. Therefore, high collection efficiency and lower pressure loss can be obtained by increasing the pore diameter of the upstream porous filter as in the coating mist processing apparatus 9 of the present invention and decreasing the pore diameter toward the downstream side.

更に低い圧力損失を得るためには図3に示すようにスリット10に整流板13を設けてフランジ構造とすることが有効である。整流板13を設けることによってスリットを通過する処理空気が下流側に流れやすくなり、その結果圧力損失を低減することができる。その際慣性作用は低下せずに働くため、塗装ミストの捕集効率は低下しない。   In order to obtain a lower pressure loss, it is effective to provide a rectifying plate 13 in the slit 10 as shown in FIG. By providing the rectifying plate 13, the processing air passing through the slit can easily flow downstream, and as a result, pressure loss can be reduced. At that time, the inertial action works without lowering, so that the collection efficiency of the paint mist does not fall.

上記本発明の塗装ミスト処理装置9を並列に並べることで処理空気の量を増やせる。具体的には図4に示すように各々の多孔質フィルタに複数のスリットを設けることで小さな塗装ミスト処理装置9を並列に並べるのと同じ構造を簡単に得ることができる。その際ジグザグの通風路を得るためにスリットの位置は前後で必ず異なるようにする。   By arranging the coating mist processing devices 9 of the present invention in parallel, the amount of processing air can be increased. Specifically, as shown in FIG. 4, by providing a plurality of slits in each porous filter, it is possible to easily obtain the same structure as arranging the small coating mist processing devices 9 in parallel. At that time, in order to obtain a zigzag ventilation path, the slit position must be different between the front and rear.

上記塗装ミスト処理装置9を導入した塗装ブースの全体図を図5に示し、以下説明する。塗装ブース14内では塗装ロボット15から塗料が噴霧され、塗装対象物16が塗装される。その際に塗装対象物16に塗着しなかった塗装ミスト17が塗装ブース14中に舞い上がる。このままでは次の塗装対象物への塗装に影響するため、循環ファン18によって速やかに塗装ブース14中の塗装ミスト17を含んだ空気をフロア19の下に吸引する。   An overall view of the painting booth in which the painting mist processing device 9 is introduced is shown in FIG. 5 and will be described below. In the painting booth 14, the paint is sprayed from the painting robot 15 and the painting object 16 is painted. At that time, the painting mist 17 that has not been applied to the painting object 16 rises in the painting booth 14. In this state, since the coating on the next object to be coated is affected, air including the coating mist 17 in the painting booth 14 is quickly sucked under the floor 19 by the circulation fan 18.

塗装ブース14から排出された処理空気は本発明の塗装ミスト処理装置9に導入され、処理空気中の塗装ミスト17が除去される。塗装ミスト17が除去された処理空気は塗料に含まれる有機溶剤の爆発限界を下回るように熱交換気ユニット20を備えた換気装置21によって一部が外気と交換された後に空調機22を通って温湿度を例えば25℃、60%RH以下に調整された状態で塗装ブース14内に戻される。   The processing air discharged from the coating booth 14 is introduced into the coating mist processing apparatus 9 of the present invention, and the coating mist 17 in the processing air is removed. The treated air from which the coating mist 17 has been removed is partially exchanged with the outside air by the ventilator 21 having the heat exchange air unit 20 so as to be below the explosion limit of the organic solvent contained in the paint, and then passes through the air conditioner 22. The temperature and humidity are returned to the painting booth 14 with the temperature and humidity adjusted to, for example, 25 ° C. and 60% RH or less.

また、空調機22を通過した後の処理空気は塗装ブース14に戻される手前でイオン発生手段28によって空気イオンが付加される。イオン発生手段は図5に示すとおり先端の尖った放電電極29と板状の対向電極30で構成されており、高圧電源31によって放電電極29に高電圧を、対向電極30に0Vを印加することによって放電を起こし、放電電極29の先端から空気イオンを発生する。   In addition, the process air after passing through the air conditioner 22 is added with air ions by the ion generating means 28 before being returned to the coating booth 14. As shown in FIG. 5, the ion generating means is composed of a discharge electrode 29 having a sharp tip and a plate-like counter electrode 30, and a high voltage is applied to the discharge electrode 29 by a high voltage power supply 31 and 0 V is applied to the counter electrode 30. To cause discharge, and generate air ions from the tip of the discharge electrode 29.

空気イオンが付着して帯電した塗装ミストは電場の作用が働いて各々の多孔質フィルタに付着捕集されやすくなる。また、帯電した塗装ミスト17が付着することによって溜まる電荷を逃がすために、各々の多孔質フィルタはアースに接続されて0Vとなっている。   The coating mist charged with air ions attached thereto is easily collected and collected by each porous filter due to the action of an electric field. Further, in order to release the electric charge accumulated by the charged coating mist 17 adhering, each porous filter is connected to the ground and becomes 0V.

次に捕集した塗装ミストを多孔質フィルタから取り除いて装置を再生する動作について図6および図7を用いて以下説明する。   Next, the operation | movement which removes the collected coating mist from a porous filter and reproduces | regenerates an apparatus is demonstrated below using FIG. 6 and FIG.

各々の多孔質フィルタの長手方向の幅W1は多孔質フィルタが横に引き出されても通風経路を構成するダクト23内に存在できるようにダクト23の幅W2の2倍の寸法で作られており、目詰まりした後は図6のように下流側から順に各々の多孔質フィルタの長手方向の幅W1の半分の長さ分(=W2)、手前側に引き出され、高圧洗浄水ノズル24から発する高圧洗浄水を当てることによって捕集した塗装ミスト17が洗浄除去される。   The width W1 in the longitudinal direction of each porous filter is made to be twice the width W2 of the duct 23 so that the porous filter can be present in the duct 23 constituting the ventilation path even if the porous filter is pulled out horizontally. After the clogging, as shown in FIG. 6, the porous filter is sequentially drawn from the downstream side by a half length (= W2) of the width W1 in the longitudinal direction of each porous filter, and is emitted from the high-pressure washing water nozzle 24. The coating mist 17 collected by applying the high-pressure washing water is washed away.

多孔質フィルタに残った洗浄水は高圧エアーノズル25から発する高圧エアーを当てることによって吹き飛ばされ、除去される。洗浄水は重力によって洗浄水受け槽26に落下し、貯められる。   The washing water remaining in the porous filter is blown off and removed by applying high-pressure air generated from the high-pressure air nozzle 25. The washing water falls and is stored in the washing water receiving tank 26 by gravity.

塗装ミストを捕集して再度目詰まりした各々の多孔質フィルタは図7のように下流側から順に今度は奥側に引き出され、捕集された塗装ミスト17が高圧洗浄水によって各々の多孔質フィルタから洗浄除去され、多孔質フィルタに残った洗浄水は高圧エアーによって吹き飛ばされる。   As shown in FIG. 7, each porous filter clogged by collecting the paint mist is pulled out from the downstream side to the back side in this order, and the collected paint mist 17 is collected by the high-pressure washing water. Wash water removed from the filter and remaining in the porous filter is blown away by high-pressure air.

このように処理空気に直接水が当たらないため、加湿せずに塗装ミスト17を処理空気から除去することが可能である。したがって塗装ミスト17が除去された処理空気は一部を外気と交換された後に塗装ブース14に再び戻すことができる。   As described above, since the water does not directly contact the processing air, it is possible to remove the coating mist 17 from the processing air without humidification. Accordingly, the processing air from which the coating mist 17 has been removed can be returned to the coating booth 14 after a part of the processing air is exchanged with the outside air.

従来の湿式処理装置では塗装ミスト17を取り除いた後の処理空気は加湿されているため全量を室外に排出する必要があり、そのため塗装ブース14の空調費が大きかった。本発明の塗装ミスト処理装置9では加湿しないで塗装ミスト17を除去することができるため、処理空気を塗装ブース内に戻せるようになり、塗装ブース14の空調費を削減することが可能となる。   In the conventional wet processing apparatus, since the processing air after removing the coating mist 17 is humidified, it is necessary to discharge the entire amount to the outside of the room, and thus the air conditioning cost of the coating booth 14 is large. Since the coating mist 17 can be removed without being humidified in the coating mist processing apparatus 9 of the present invention, the processing air can be returned into the coating booth, and the air conditioning cost of the coating booth 14 can be reduced.

(実施例)
図3で説明した、整流板13を設けた実施形態の塗装ミスト処理装置の捕集効率および圧力損失を測定した。以下、この装置を実施ユニットと称する。実施ユニットの開口寸法は104mm□とした。また、図3の記載寸法である各多孔質フィルタの厚みAは10mmとした。同様に整流板13のはみ出し寸法Bは5mm、各多孔質フィルタ間の距離Cは25mmとした。
(Example)
The collection efficiency and pressure loss of the coating mist processing apparatus according to the embodiment provided with the current plate 13 described in FIG. 3 were measured. Hereinafter, this apparatus is referred to as an implementation unit. The opening size of the implementation unit was 104 mm □. Further, the thickness A of each porous filter having the dimensions shown in FIG. 3 was set to 10 mm. Similarly, the protruding dimension B of the rectifying plate 13 was 5 mm, and the distance C between the porous filters was 25 mm.

中央に位置するスリット10の寸法Dは30mm、両端に位置するスリット10の一つあたりの寸法Eはその半分の15mmとした。多孔質フィルタAaおよびBaの孔27の径は3mm、多孔質フィルタAbおよびBbの孔27の径は2mm、多孔質フィルタAcおよびBcの孔27の径は1.3mm、多孔質フィルタAdおよびBdの孔27の径は0.9mmとした。   The dimension D of the slit 10 located at the center was 30 mm, and the dimension E per slit 10 located at both ends was 15 mm, which is half of that. The diameter of the holes 27 of the porous filters Aa and Ba is 3 mm, the diameter of the holes 27 of the porous filters Ab and Bb is 2 mm, the diameter of the holes 27 of the porous filters Ac and Bc is 1.3 mm, and the porous filters Ad and Bd The diameter of the hole 27 was 0.9 mm.

ここで、整流板13のはみ出し寸法Bの目安は各多孔質フィルタの厚みAの0.5〜1倍程度とすることで装置を無駄に大きくさせずに十分な整流効果が得られる。各多孔質フィルタ間の距離Cは中央に位置するスリット10の寸法Eの0.5〜1.5倍に整流板13のはみ出し寸法を足した数値とすることで圧力損失の増大を防ぐとともに塗装ミストの慣性作用による衝突効果も得ることができる。   Here, a rough rectifying effect can be obtained without unnecessarily enlarging the apparatus by setting the guideline of the protruding dimension B of the rectifying plate 13 to about 0.5 to 1 times the thickness A of each porous filter. The distance C between the porous filters is a value obtained by adding 0.5 to 1.5 times the dimension E of the slit 10 located at the center and the protruding dimension of the rectifying plate 13, thereby preventing an increase in pressure loss and painting. A collision effect due to the inertial action of the mist can also be obtained.

また、比較対象として図8に示すような、多孔質フィルタの代わりに空気が中を通過できない壁板33を用いた塗装ミスト処理装置を作成し、同様に捕集効率と圧力損失を測定した。この装置を比較ユニット32と称する。壁の厚みAは実施ユニットの多孔質フィルタ同様に10mmであり、その他寸法も実施ユニットと同じである。   Further, as shown in FIG. 8, a coating mist processing apparatus using a wall plate 33 in which air cannot pass through instead of the porous filter as shown in FIG. 8 was created, and the collection efficiency and pressure loss were measured in the same manner. This device is referred to as a comparison unit 32. The wall thickness A is 10 mm as in the porous filter of the implementation unit, and the other dimensions are the same as those of the implementation unit.

風速2.9m/sの条件で吸込み口から塗装ミストを含む空気を吸引させた時の、それぞれのユニットの捕集効率と圧力損失の結果を図9に示す。図9に示すとおり比較ユニットの捕集効率は高くても65%に対して実施ユニットは90%の捕集効率を得ている。   FIG. 9 shows the results of the collection efficiency and pressure loss of each unit when the air containing the paint mist was sucked from the suction port under the condition of the wind speed of 2.9 m / s. As shown in FIG. 9, even if the collection efficiency of the comparison unit is high, the implementation unit obtains a collection efficiency of 90% with respect to 65%.

また、比較ユニットの圧力損失は1700Pa前後であるのに対して実施ユニットの圧力損失は初期で340Pa、塗装ミスト噴霧量50g到達時で800Paとなっており、常に比較ユニットよりも大幅に低い値となった。この測定結果が示すとおり、本発明の塗装ミスト処理装置は従来の装置よりも高い捕集効率と低い圧力損失が得られることがわかった。   In addition, the pressure loss of the comparison unit is around 1700 Pa, whereas the pressure loss of the implementation unit is 340 Pa at the beginning and 800 Pa when the coating mist spray amount reaches 50 g, which is always much lower than the comparison unit. became. As shown by the measurement results, it was found that the coating mist processing apparatus of the present invention can obtain higher collection efficiency and lower pressure loss than the conventional apparatus.

本発明にかかる塗装ミスト処理装置は、加湿や目詰まりをせずに高い塗装ミスト捕集効率と低い圧力損失を得られるので、自動車や家電製品などの塗装工程で使用される塗装ブース内の空調費を削減することが可能な塗装品質維持装置として有用である。   The coating mist processing apparatus according to the present invention can achieve high coating mist collection efficiency and low pressure loss without humidification or clogging, so that the air conditioning in the coating booth used in the coating process of automobiles and home appliances, etc. It is useful as a paint quality maintenance device that can reduce costs.

1 多孔質フィルタAa
2 多孔質フィルタBa
3 多孔質フィルタAb
4 多孔質フィルタBb
5 多孔質フィルタAc
6 多孔質フィルタBc
7 多孔質フィルタAd
8 多孔質フィルタBd
9 塗装ミスト処理装置
10 スリット
11 通風方向
12 空気の流れ
13 整流板
14 塗装ブース
15 塗装ロボット
16 塗装対象物
17 塗装ミスト
18 循環ファン
19 フロア
20 熱交換気ユニット
21 換気装置
22 空調機
23 ダクト
24 高圧洗浄水ノズル
25 高圧エアーノズル
26 洗浄水受け槽
27 孔
28 イオン発生手段
29 放電電極
30 対向電極
31 高圧電源
32 比較ユニット
33 壁板
1 Porous filter Aa
2 Porous filter Ba
3 Porous filter Ab
4 Porous filter Bb
5 Porous filter Ac
6 Porous filter Bc
7 Porous filter Ad
8 Porous filter Bd
DESCRIPTION OF SYMBOLS 9 Coating mist processing apparatus 10 Slit 11 Ventilation direction 12 Air flow 13 Rectifying plate 14 Coating booth 15 Coating robot 16 Coating object 17 Coating mist 18 Circulating fan 19 Floor 20 Heat exchange air unit 21 Ventilator 22 Air conditioner 23 Duct 24 High pressure Washing water nozzle 25 High pressure air nozzle 26 Washing water receiving tank 27 Hole 28 Ion generating means 29 Discharge electrode 30 Counter electrode 31 High voltage power supply 32 Comparison unit 33 Wall plate

Claims (4)

塗装ブースから排出された塗装ミストを含んだ空気を処理して前記塗装ブースに戻す通風経路内に設置される塗装ミスト処理装置であってともに空気が通過できる多孔質板状の金属もしくはセラミックスからなる、通風方向から見て異なる位置にスリットを有する多孔質フィルタAおよび多孔質フィルタBとを通風方向に一定の間隔を設けながら交互に積層し、前記スリットの壁に通風方向上流側から下流側に向けてはみ出した整流板を設けた塗装ミスト処理装置 A paint mist processing unit that will be installed in the process the air containing the discharged paint mist from paint booth ventilation path back to the painting booth, from both a porous plate-shaped metal or ceramic which air can pass The porous filter A and the porous filter B having slits at different positions when viewed from the ventilation direction are alternately stacked while providing a certain interval in the ventilation direction, and the slit wall is upstream of the ventilation direction from the downstream side. Paint mist processing equipment with a rectifying plate that protrudes toward the surface . 整流板のはみ出し寸法は多孔質フィルタの厚みの0.5〜1倍、各多孔質フィルタ間の距離は中央に位置するスリットの寸法の0.5〜1.5倍に前記整流板のはみ出し寸法を足した数値とした請求項1記載の塗装ミスト処理装置 The protruding dimension of the rectifying plate is 0.5 to 1 times the thickness of the porous filter, and the distance between each porous filter is 0.5 to 1.5 times the dimension of the slit located at the center. The coating mist processing apparatus according to claim 1, which is a numerical value obtained by adding スリットの寸法は、多孔質フィルタの孔径よりも大きくした請求項1記載の塗装ミスト処理装置 The coating mist processing apparatus according to claim 1, wherein a dimension of the slit is larger than a hole diameter of the porous filter . 風速2.9m/sの空気を吸引させ、塗装ミストの捕集を行なう請求項1から3のいずれか一項に記載の塗装ミスト処理装置。 The coating mist processing apparatus according to any one of claims 1 to 3, wherein air at a wind speed of 2.9 m / s is sucked to collect the coating mist.
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