JP6780276B2 - Paint mist treatment device - Google Patents
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- JP6780276B2 JP6780276B2 JP2016065144A JP2016065144A JP6780276B2 JP 6780276 B2 JP6780276 B2 JP 6780276B2 JP 2016065144 A JP2016065144 A JP 2016065144A JP 2016065144 A JP2016065144 A JP 2016065144A JP 6780276 B2 JP6780276 B2 JP 6780276B2
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本発明は、塗装作業などで発生する塗料成分なら成る塗料ミストを含有するガスから塗料成分を除去する塗料成分処理装置に関する。 The present invention relates to a paint component processing apparatus that removes a paint component from a gas containing a paint mist, which is a paint component generated in a painting operation or the like.
従来、塗料を用いた塗装設備において塗装作業をする場合、余剰の塗料成分が室内空気に残存するため、作業衛生上の問題から室内を換気する塗装ブースが設けられている。この塗装ブースからは塗料成分で構成される塗料ミストを含有する排気ガスが系外に排出されるため、環境汚染や公害の原因となる。そのため排気ガスから塗料成分を分離除去する検討が行われてきた。 Conventionally, when painting work is performed in a painting facility using paint, a painting booth is provided to ventilate the room due to work hygiene problems because excess paint components remain in the room air. Exhaust gas containing paint mist composed of paint components is discharged from this painting booth to the outside of the system, which causes environmental pollution and pollution. Therefore, studies have been conducted to separate and remove paint components from exhaust gas.
塗料成分を分離除去する手段としては、洗浄水に接触させて塗料成分を捕集する湿式法(例えば、特許文献1参照)、または、フィルタ、バッファなどに接触させて塗料成分を捕集して除去する乾式法(例えば、特許文献2参照)が挙げられる。 As a means for separating and removing the paint component, a wet method (see, for example, Patent Document 1) in which the paint component is collected by contacting with washing water, or a filter, a buffer, or the like is used to collect the paint component. Examples thereof include a dry method for removing (see, for example, Patent Document 2).
しかしながら、湿式法を用いた場合には、大量の塗料成分含有排水の処理が別途必要であり、排気ガスを循環させて塗装作業場へ供給する場合に湿度が高くなるという問題がある。また、湿式法における塗料成分含有排水の処理工程は複雑である。そのため、乾式法による塗料成分除去が注目されている。中でも繊維状フィルタを用いた塗料成分除去が多くの塗装設備で採用されている。 However, when the wet method is used, it is necessary to separately treat a large amount of wastewater containing a paint component, and there is a problem that the humidity becomes high when the exhaust gas is circulated and supplied to the painting work place. In addition, the process of treating wastewater containing paint components in the wet method is complicated. Therefore, attention is being paid to the removal of paint components by the dry method. Among them, the removal of paint components using a fibrous filter is adopted in many painting facilities.
ところが、従来の繊維状フィルタを使用した塗料成分除去では、繊維の深層部で捕集された付着性の高い塗料成分を脱離してフィルタを再生することは非常に困難である。そのため繊維状フィルタを頻繁に交換しなければならず、資源の過剰消費や多くの交換作業工数が必要となる。 However, in the removal of paint components using a conventional fibrous filter, it is very difficult to regenerate the filter by removing the highly adhesive paint components collected in the deep part of the fiber. Therefore, the fibrous filter must be replaced frequently, which requires excessive resource consumption and a large number of replacement work man-hours.
そこで、本発明は上記の問題点に鑑みてなされたものであって、その目的は、塗料成分を十分除去できる上、フィルタの交換を不要にできあるいは抑制でき、資源を節約できる塗料ミスト処理装置を提供することにある。 Therefore, the present invention has been made in view of the above problems, and an object of the present invention is a paint mist treatment apparatus capable of sufficiently removing paint components, eliminating or suppressing filter replacement, and saving resources. Is to provide.
上記の課題を解決するため、本発明者等が鋭意研究した結果、ついに本発明を完成するに到った。すなわち、本発明は以下の通りである。
(1)塗料成分を付着するフィルタ粒子が充填され、該塗料成分から成る塗料ミストを含有する塗料ミスト含有ガスを導入することで、該塗料成分を前記フィルタ粒子に付着させて除去し、塗料成分が除去された処理済ガスを排出する粒子充填槽と、前記塗料成分が付着したフィルタ粒子から該塗料成分を脱離する脱離部と、前記粒子充填槽から前記離脱部へフィルタ粒子を排出させる粒子排出部と、前記脱離部にて脱離された塗料成分とフィルタ粒子とを分離する分離部と、前記分離部にて分離されたフィルタ粒子を再び前記粒子充填槽へ充填する循環路と、を備えた塗料ミスト処理装置。
As a result of diligent research by the present inventors in order to solve the above problems, the present invention has finally been completed. That is, the present invention is as follows.
(1) The filter particles to which the paint component is attached are filled, and by introducing a paint mist-containing gas containing the paint mist composed of the paint component, the paint component is attached to the filter particles and removed, and the paint component is removed. A particle filling tank that discharges the treated gas from which the particles have been removed, a desorption portion that desorbs the paint component from the filter particles to which the paint component is attached, and a desorption portion that discharges the filter particles from the particle filling tank to the desorption portion. A particle discharge part, a separation part for separating the paint component and the filter particles desorbed at the desorption part, and a circulation path for refilling the particle filling tank with the filter particles separated at the separation part. A paint mist treatment device equipped with.
上記構成によると、塗料ミスト含有ガスに含まれる塗料成分を粒子フィルタで十分除去できる上、粒子フィルタを再生して循環させることで繰り返し使用できることから、フィルタの交換を必要とせず、資源を節約できる。 According to the above configuration, the paint component contained in the paint mist-containing gas can be sufficiently removed by the particle filter, and the particle filter can be regenerated and circulated for repeated use, so that the filter does not need to be replaced and resources can be saved. ..
(2)前記塗料ミスト含有ガスの前記粒子充填槽への導入方向と、前記フィルタ粒子の前記粒子充填槽内での流動方向とが、垂直関係にある(1)の塗料ミスト処理装置。
(3)前記フィルタ粒子として、重量の異なる2種類以上のフィルタ粒子を使用する(1)または(2)の塗料ミスト処理装置。
(4)前記脱離部は、塗料成分が付着したフィルタ粒子同士の衝突により、フィルタ粒子から塗料成分を脱離させる(1)から(3)のいずれか1つの塗料ミスト処理装置。
(5)前記脱離部は、表面に凹凸形状を有する凹凸部を備え、塗料成分が付着したフィルタ粒子を該凹凸部の表面に接触させてフィルタ粒子から塗料成分を脱離させる(1)から(4)のいずれか1つの塗料ミスト処理装置。
(6)前記脱離部は、加熱処理により塗料フィルタ粒子から塗料成分を脱離させる(1)から(5)のいずれか1つの塗料ミスト処理装置。
(7)前記分離部は、フィルタ粒子と脱離された塗料成分とに高風速ガスを通気させ、重量差によって両者を分離する(1)から(6)のいずれか1つの塗料ミスト処理装置。
(8)前記分離部は、フィルタ粒子と脱離された塗料成分とを液体に浸漬させて比重差によって両者を分離する(1)から(7)のいずれか1つの塗料ミスト処理装置。
(9)塗料成分から成る塗料ミストを含有する塗料ミスト含有ガスをフィルタ粒子に接触させ、該塗料成分を前記フィルタ粒子に付着させて除去し、塗料成分が除去された処理済ガスを排出する排出工程と、前記塗料成分が付着したフィルタ粒子から該塗料成分を脱離する脱離工程と、前記脱離工程にて脱離された塗料成分とフィルタ粒子とを分離する分離工程と、前記分離工程にて分離されたフィルタ粒子を再び前記排出工程で用いるように循環させる循環工程と、を含むことを特徴とする塗料ミスト処理方法。
(2) The paint mist treatment apparatus according to (1), wherein the direction of introducing the paint mist-containing gas into the particle filling tank and the direction of flow of the filter particles in the particle filling tank are in a vertical relationship.
(3) The paint mist treatment apparatus according to (1) or (2), which uses two or more types of filter particles having different weights as the filter particles.
(4) The desorption portion is a paint mist treatment apparatus according to any one of (1) to (3), which desorbs a paint component from the filter particles by collision between filter particles to which the paint component is attached.
(5) The detached portion is provided with an uneven portion having an uneven shape on the surface, and the filter particles to which the paint component is attached are brought into contact with the surface of the uneven portion to desorb the paint component from the filter particles (1). (4) Any one of the paint mist treatment devices.
(6) The desorbed portion is a paint mist treatment apparatus according to any one of (1) to (5), which desorbs a paint component from paint filter particles by heat treatment.
(7) The separation unit is a paint mist treatment apparatus according to any one of (1) to (6), wherein a high wind speed gas is ventilated through the filter particles and the desorbed paint component, and the two are separated by a weight difference.
(8) The separation unit is a paint mist treatment apparatus according to any one of (1) to (7), wherein the filter particles and the desorbed paint component are immersed in a liquid to separate them by a difference in specific gravity.
(9) A paint mist-containing gas containing a paint mist composed of a paint component is brought into contact with the filter particles, the paint component is attached to the filter particles and removed, and the treated gas from which the paint component has been removed is discharged. A step, a desorption step of desorbing the paint component from the filter particles to which the paint component is attached, a separation step of separating the paint component desorbed in the desorption step and the filter particles, and the separation step. A coating mist treatment method comprising a circulation step of circulating the filter particles separated in the above step again so as to be used in the discharge step.
本発明に係る塗料ミスト処理装置によれば、塗料ミスト含有ガスに含まれる塗料成分を粒子フィルタで十分除去できる上、粒子フィルタを再生して循環させることで繰り返し使用できるため、フィルタの交換を必要とせず、資源を節約できる。 According to the paint mist treatment apparatus according to the present invention, the paint component contained in the paint mist-containing gas can be sufficiently removed by the particle filter, and the particle filter can be regenerated and circulated for repeated use, so that the filter needs to be replaced. You can save resources without doing so.
以下、発明を実施する形態について、図面を参照して詳細に説明する。以下に示す実施の形態において、個数、量などに言及する場合、特に記載がある場合を除き、本発明の範囲は必ずしもその個数、量などに限定されない。 Hereinafter, embodiments according to the invention will be described in detail with reference to the drawings. In the embodiments shown below, when the number, quantity, etc. are referred to, the scope of the present invention is not necessarily limited to the number, quantity, etc., unless otherwise specified.
図1は、本実施形態の塗料ミスト処理装置10の構成の一例を示す構成図である。図1に示すように、塗料ミスト処理装置10は、フィルタ粒子1が充填された粒子充填槽2と、粒子排出部3と、脱離部4と、分離部5と、循環路7とを備えている。 FIG. 1 is a configuration diagram showing an example of the configuration of the paint mist treatment apparatus 10 of the present embodiment. As shown in FIG. 1, the paint mist treatment device 10 includes a particle filling tank 2 filled with filter particles 1, a particle discharging section 3, a desorbing section 4, a separating section 5, and a circulation path 7. ing.
粒子充填槽2は、フィルタ粒子1が充填される槽である。フィルタ粒子1が充填された粒子充填槽2に塗料成分から成る塗料ミストを含有する塗料ミスト含有ガスを導入し、フィルタ粒子1に接触させると、フィルタ粒子1により塗料成分が付着除去され、粒子充填槽2から処理済ガスが排出される。 The particle filling tank 2 is a tank in which the filter particles 1 are filled. When a paint mist-containing gas containing a paint mist composed of a paint component is introduced into a particle filling tank 2 filled with the filter particles 1 and brought into contact with the filter particles 1, the paint component is adhered and removed by the filter particles 1 to fill the particles. The treated gas is discharged from the tank 2.
粒子充填槽2において、フィルタ粒子1と塗料ミスト含有ガスとの接触面(塗料ミスト含有ガスの導入口)の間には網またはパンチングメタルなどが設置され、塗料ミスト含有ガスが均一に導入されるよう、厚みが一定に保たれている。網またはパンチングメタルの材質は特に限定されず、例えば、アルミ、鉄、ステンレスを用いてもよい。なお、塗料ミスト含有ガスの発生源から粒子充填槽2までは図示しないダクトで囲まれており、塗料ミスト含有ガスが拡散されないようになっている。 In the particle filling tank 2, a net or a punching metal is installed between the contact surface between the filter particles 1 and the paint mist-containing gas (the introduction port of the paint mist-containing gas), and the paint mist-containing gas is uniformly introduced. The thickness is kept constant. The material of the net or the punching metal is not particularly limited, and for example, aluminum, iron, or stainless steel may be used. The source of the paint mist-containing gas to the particle filling tank 2 is surrounded by a duct (not shown) so that the paint mist-containing gas is not diffused.
また、粒子充填槽2における処理済ガスの排出口(排気側)も同様に、網またはパンチングメタルなどが設置され、処理済ガスが排出されるように構成されている。また、粒子充填槽2における処理済ガスの排出口も図示しないダクトと接続している。 Further, the discharge port (exhaust side) of the treated gas in the particle filling tank 2 is similarly provided with a net, a punching metal, or the like so that the treated gas is discharged. Further, the discharged port of the treated gas in the particle filling tank 2 is also connected to a duct (not shown).
フィルタ粒子1は、塗料成分を吸着(付着)により捕集する粒子である。吸着は、その方法は限定されず、化学的吸着であっても物理的吸着であってもこれらの組み合わせであってもよい。フィルタ粒子1は、球状であることが好ましい。球状であることにより塗料ミスト処理装置10内を滑らかに流動可能となり、フィルタ粒子1の詰まり等による装置故障を抑制できる。フィルタ粒子1の材質は特に限定しないが、塗料成分を吸着できる材料、具体的には、アルミナ、ナイロン、ステンレス、セラミック、ジルコニア、瑪瑙、PTFE、ポリプロピレン、ポリエチレン、タングステン、クロム、鋼、ガラスのうち少なくとも1つを含んで構成されることが好ましい。 The filter particles 1 are particles that collect paint components by adsorption (adhesion). The method of adsorption is not limited, and it may be chemical adsorption, physical adsorption, or a combination thereof. The filter particles 1 are preferably spherical. Since it is spherical, it can flow smoothly in the paint mist treatment device 10, and it is possible to suppress device failure due to clogging of the filter particles 1. The material of the filter particle 1 is not particularly limited, but among materials capable of adsorbing paint components, specifically, alumina, nylon, stainless steel, ceramic, zirconia, amber, PTFE, polypropylene, polyethylene, tungsten, chromium, steel, and glass. It is preferable to include at least one.
塗料ミスト処理装置10では、フィルタ粒子1として、質量の異なる二種類以上のフィルタ粒子を使用することが好ましい。粒径の小さい塗料ミストを含有する塗料ミスト含有ガスを処理対象とする場合、フィルタ粒子1の平均粒径もまた小さく設計する必要がある。その場合フィルタ粒子1の重量が小さくなり、後段の脱離部4において脱離に必要なエネルギーが得られない可能性がある。そこで質量の比較的大きいフィルタ粒子1を混入して充填することにより、脱離部4での脱離に必要なエネルギーが得られ、効率よく塗料成分をフィルタ粒子から脱離することができる。 In the paint mist treatment apparatus 10, it is preferable to use two or more types of filter particles having different masses as the filter particles 1. When a paint mist-containing gas containing a paint mist having a small particle size is to be treated, it is necessary to design the average particle size of the filter particles 1 to be small as well. In that case, the weight of the filter particles 1 becomes small, and there is a possibility that the energy required for desorption cannot be obtained in the desorption portion 4 in the subsequent stage. Therefore, by mixing and filling the filter particles 1 having a relatively large mass, the energy required for desorption at the desorption portion 4 can be obtained, and the paint component can be efficiently desorbed from the filter particles.
粒子充填槽2に導入される塗料ミストの粒径によってフィルタ粒子の粒径(平均粒径)を適切に設計し、また、適切な圧力損失になるように粒子充填槽2の厚みを設計することで、塗料ミスト処理装置10は、いかなる塗料ミストにおいても対応することができる。例えば、粒径の小さい塗料ミストを捕集するためには、フィルタ粒子1の平均粒径を小さくし、圧力損失を高い値となるように粒子充填槽2の厚みを設計すればよい。 Appropriately design the particle size (average particle size) of the filter particles according to the particle size of the paint mist introduced into the particle filling tank 2, and design the thickness of the particle filling tank 2 so as to obtain an appropriate pressure loss. Therefore, the paint mist processing device 10 can handle any paint mist. For example, in order to collect paint mist having a small particle size, the thickness of the particle filling tank 2 may be designed so that the average particle size of the filter particles 1 is reduced and the pressure loss is high.
粒子排出部3は、塗料成分が付着したフィルタ粒子1を粒子充填槽2から排出する排出処理を行う。 The particle discharge unit 3 performs a discharge process of discharging the filter particles 1 to which the paint component is attached from the particle filling tank 2.
粒子排出部3は、例えば、フィルタ粒子1を収容する空間を複数有する回転体構造をとり、その空間が粒子充填槽2側から脱離部4側へ回転するように構成されていてもよい。粒子排出部3を粒子充填槽の下方に設置することで、粒子充填槽2内のフィルタ粒子1が自重で粒子排出部3の空間へ自動的に収容される。具体例としては、粒子排出部3は、粒子充填槽2の下流に接続したケースあるいは粒子充填槽2の下端の一部であるケースと、ケース内で回転するロータリーバルブとを備えた構成が挙げられるが、これに限定されない。 The particle discharge unit 3 may have, for example, a rotating body structure having a plurality of spaces for accommodating the filter particles 1, and the space may be configured to rotate from the particle filling tank 2 side to the desorption portion 4 side. By installing the particle discharging unit 3 below the particle filling tank, the filter particles 1 in the particle filling tank 2 are automatically accommodated in the space of the particle discharging unit 3 by their own weight. As a specific example, the particle discharge unit 3 includes a case connected to the downstream of the particle filling tank 2 or a part of the lower end of the particle filling tank 2, and a rotary valve rotating in the case. However, it is not limited to this.
粒子排出部3が駆動することで、フィルタ粒子1は粒子充填槽2内を上部から下部へ流動する。フィルタ粒子1は、粒子充填槽2の上部から再充填され、下部に移動する程多くの塗料成分を付着する。フィルタ粒子1は粒子排出部3によって粒子充填槽2から排出され、搬送ラインL1から脱離部4に導入される。搬送ラインL1では、塗料成分が付着したフィルタ粒子1は、例えば、自重により搬送されるが、別の搬送方法を用いてもよい。 When the particle discharge unit 3 is driven, the filter particles 1 flow in the particle filling tank 2 from the upper part to the lower part. The filter particles 1 are refilled from the upper part of the particle filling tank 2, and more paint components are attached as they move to the lower part. The filter particles 1 are discharged from the particle filling tank 2 by the particle discharge unit 3 and introduced into the desorption unit 4 from the transport line L1. In the transport line L1, the filter particles 1 to which the paint component is attached are transported by their own weight, for example, but another transport method may be used.
粒子充填槽2内のフィルタ粒子1の移動速度は塗料ミストの濃度に依存する。そのため、粒子排出部3にてフィルタ粒子1の排出速度を変更できるのが好ましい。例えば、フィルタ粒子1の目詰まりが早ければ排出速度を速める、といったように対処することができる。 The moving speed of the filter particles 1 in the particle filling tank 2 depends on the concentration of the paint mist. Therefore, it is preferable that the particle discharge unit 3 can change the discharge rate of the filter particles 1. For example, if the filter particles 1 are clogged quickly, the discharge rate can be increased.
塗料ミスト処理装置10では、塗料ミスト含有ガスを粒子充填槽2に導入する方向と、フィルタ粒子1の充填および排出によりフィルタ粒子1が流動する方向とを垂直関係にすることで粒子充填槽2の構造をより簡素にできる。 In the paint mist treatment apparatus 10, the direction in which the paint mist-containing gas is introduced into the particle filling tank 2 and the direction in which the filter particles 1 flow due to the filling and discharging of the filter particles 1 are made vertical to each other in the particle filling tank 2. The structure can be made simpler.
脱離部4は、フィルタ粒子1に付着した塗料成分を脱離させる脱離処理を行う。脱離処理は、化学的処理であっても物理的処理であってもこれらの組み合わせであってもよい。フィルタ粒子1は粒子排出部3により粒子充填槽2から流動的に排出される。そのため、粒子充填槽1の下層部に位置していたフィルタ粒子1が脱離部4で露出され、離脱部4にて容易に化学的および/または物理的応力を加えることができる。 The desorption portion 4 performs a desorption treatment for desorbing the paint component adhering to the filter particles 1. The desorption treatment may be a chemical treatment, a physical treatment, or a combination thereof. The filter particles 1 are fluidly discharged from the particle filling tank 2 by the particle discharge unit 3. Therefore, the filter particles 1 located in the lower layer portion of the particle filling tank 1 are exposed at the detachment portion 4, and chemical and / or physical stress can be easily applied at the detachment portion 4.
脱離部4は、塗料成分が付着したフィルタ粒子1同士を衝突させる構造であってもよい。このような構造であると、フィルタ粒子1同士の衝突により加えられた振動により、フィルタ粒子1から塗料成分を効果的に脱離できる。図2は、塗料ミスト処理装置10の脱離部4の一例を示す図である。図2に示す脱離部4は、例えばドラム形状を有し廻旋運動を行う。塗料成分8を吸着したフィルタ粒子1は回旋する脱離部4内に導入され、脱離部4の回旋運動により、フィルタ粒子1同士の衝突が生じ、付着した塗料成分8が脱離する。 The detached portion 4 may have a structure in which the filter particles 1 to which the paint component is attached collide with each other. With such a structure, the paint component can be effectively desorbed from the filter particles 1 by the vibration applied by the collision between the filter particles 1. FIG. 2 is a diagram showing an example of a detachment portion 4 of the paint mist treatment device 10. The detaching portion 4 shown in FIG. 2 has, for example, a drum shape and performs a rotational movement. The filter particles 1 adsorbing the paint component 8 are introduced into the rotating detachable portion 4, and the rotational movement of the detachable portion 4 causes collisions between the filter particles 1 and the adhered paint component 8 is detached.
または、脱離部4は、塗料成分が付着したフィルタ粒子1を凹凸状表面に接触させる構造であってもよい。このような構造であると、凸凹状表面に接触させることによりフィルタ粒子に摩擦力が加わり、塗料成分を効果的に脱離できる。図3は、塗料ミスト処理装置10の脱離部4の別の一例を示す図である。図3に示す脱離部4には、その内部に凸凹状表面を有する凹凸部9が形成されている。塗料成分8を吸着したフィルタ粒子1は凸凹部9を有する脱離部4に導入され、凸凹部9とフィルタ粒子1が接触することでフィルタ粒子1に摩擦力が加わり塗料成分8が脱離される。 Alternatively, the detached portion 4 may have a structure in which the filter particles 1 to which the paint component is attached are brought into contact with the uneven surface. With such a structure, a frictional force is applied to the filter particles by bringing them into contact with the uneven surface, and the paint component can be effectively desorbed. FIG. 3 is a diagram showing another example of the detachment portion 4 of the paint mist treatment device 10. The detached portion 4 shown in FIG. 3 is formed with an uneven portion 9 having an uneven surface inside. The filter particle 1 adsorbing the paint component 8 is introduced into the detaching portion 4 having the unevenness 9, and when the unevenness 9 and the filter particle 1 come into contact with each other, a frictional force is applied to the filter particle 1 and the paint component 8 is detached. ..
あるいは、脱離部4は、塗料成分8が付着したフィルタ粒子1を加熱処理する構造でもよい。塗料成分の付着性が高い場合、振動や摩擦といった物理的処理だけでは容易に塗料成分を脱離できない可能性がある。フィルタ粒子を加熱処理する構造とすることにより、付着性成分を揮発または分解または変性させ、塗料成分を硬化させることができる。 Alternatively, the detached portion 4 may have a structure in which the filter particles 1 to which the paint component 8 is attached are heat-treated. If the paint component has high adhesiveness, it may not be possible to easily remove the paint component only by physical treatment such as vibration or friction. By adopting a structure in which the filter particles are heat-treated, the adhesive component can be volatilized, decomposed or denatured, and the paint component can be cured.
また、脱離部4は、図2に示す構造と図3に示す構図と加熱処理する構成とのいずれか2つ以上を組み合わせたものであってもよい。もちろん、脱離部4は、開示した構造に限定されない。 Further, the detachable portion 4 may be a combination of any two or more of the structure shown in FIG. 2, the composition shown in FIG. 3, and the configuration to be heat-treated. Of course, the detachable portion 4 is not limited to the disclosed structure.
図1に戻って塗料ミスト処理装置1の説明を続ける。脱離部4にてフィルタ粒子1から塗料成分が脱離された後、フィルタ粒子1と塗料成分との混合物は搬送ラインL2を通り、分離部5に導入される。搬送ラインL2は、上記混合物を、例えば、コンベア式搬送、エア式搬送、または自重落下等により、搬送する。 Returning to FIG. 1, the description of the paint mist treatment device 1 will be continued. After the paint component is desorbed from the filter particles 1 by the desorption portion 4, the mixture of the filter particles 1 and the paint component passes through the transport line L2 and is introduced into the separation portion 5. The transport line L2 transports the mixture by, for example, conveyor-type transport, air-type transport, or self-weight drop.
分離部5は、フィルタ粒子1と塗料成分との分離処理を行う。 The separation unit 5 separates the filter particles 1 and the paint component.
分離部5は、フィルタ粒子1及び脱離された塗料成分に高風速ガスを通気させ、重量差によってフィルタ粒子と塗料成分とを分離する構造であってもよい。この構造は、フィルタ粒子1の重量が塗料成分の重量よりも比較的大きい場合に好適に用いることができる。分離された塗料成分は搬送ラインL5を通り、塗料回収部6に収容される。分離部5が上記高風速ガスを用いる上記構造の場合、搬送ラインL5は高風速ガスの流路である。 The separation unit 5 may have a structure in which the filter particles 1 and the desorbed paint component are ventilated with a high wind speed gas, and the filter particles and the paint component are separated by a weight difference. This structure can be preferably used when the weight of the filter particles 1 is relatively larger than the weight of the paint component. The separated paint component passes through the transport line L5 and is stored in the paint recovery unit 6. When the separation unit 5 has the above structure using the high wind speed gas, the transfer line L5 is a flow path for the high wind speed gas.
あるいは、分離部5は、フィルタ粒子1と脱離された塗料成分とを液体に浸漬させ、比重差によってフィルタ粒子と塗料成分とを分離する構造であってもよい。この構造は、フィルタ粒子1の比重が上記液体よりも比較的大きく、上記液体の比重が塗料成分よりも比較的大きい場合に、好適に用いることができる。この構造であると、フィルタ粒子1は上記液体中に沈殿し、塗料成分は上記液体表面に分離され、容易に回収できる。上記液体表面に分離された塗料成分は、例えば送液ポンプで上記液体の一部と共に搬送ラインL5に搬送され、塗料回収部6に収容される。 Alternatively, the separation unit 5 may have a structure in which the filter particles 1 and the desorbed paint component are immersed in a liquid, and the filter particles and the paint component are separated by a difference in specific gravity. This structure can be preferably used when the specific gravity of the filter particles 1 is relatively larger than that of the liquid and the specific gravity of the liquid is relatively larger than that of the paint component. With this structure, the filter particles 1 are precipitated in the liquid, and the paint component is separated on the liquid surface and can be easily recovered. The paint component separated on the surface of the liquid is conveyed to the transfer line L5 together with a part of the liquid by, for example, a liquid feed pump, and is housed in the paint recovery unit 6.
分離部5にて塗料成分と分離されたフィルタ粒子1は、搬送ラインL3を通り、搬送路7に導入される。搬送ラインL3は、フィルタ粒子1を、例えば、コンベア式搬送、エア式搬送、または自重落下等により、搬送する。 The filter particles 1 separated from the paint component by the separation unit 5 pass through the transport line L3 and are introduced into the transport path 7. The transport line L3 transports the filter particles 1 by, for example, conveyor type transport, air type transport, or self-weight drop.
循環路7は、分離部6にて分離されたフィルタ粒子1を、搬送ラインL4を通して再び粒子充填槽2へ充填する。循環路7の搬送形式としては、自動でフィルタ粒子1を粒子充填槽2に再充填することができるコンベア式や、高風速ガスによってフィルタ粒子1を粒子充填槽2に搬送するエア式を用いることができるが、これらには限定されない。 The circulation path 7 refills the particle filling tank 2 with the filter particles 1 separated by the separation section 6 through the transport line L4. As the transport type of the circulation path 7, a conveyor type that can automatically refill the filter particles 1 into the particle filling tank 2 or an air type that transports the filter particles 1 to the particle filling tank 2 by a high wind velocity gas is used. However, it is not limited to these.
循環路7で搬送されたフィルタ粒子1は、搬送ラインL4を通って粒子充填槽2へ再充填される。粒子充填槽2へ充填されたフィルタ粒子1は塗料ミスト含有ガスから塗料成分を再び捕集する。以降は上記の動作を繰り返す。このように、塗料ミスト処理装置10は、フィルタ粒子1による塗料成分の捕集、脱離、分離、再充填を連続して行うことで、塗装ミストの連続除去を可能としている。 The filter particles 1 transported in the circulation path 7 are refilled in the particle filling tank 2 through the transport line L4. The filter particles 1 filled in the particle filling tank 2 collect the paint component again from the paint mist-containing gas. After that, the above operation is repeated. As described above, the paint mist treatment apparatus 10 can continuously remove the paint mist by continuously collecting, desorbing, separating, and refilling the paint component by the filter particles 1.
なお、本実施形態では、塗装ミスト処理装置10が実施する各工程を詳細に説明するため脱離部4と分離部5とを分割して説明しているが、脱離部4と分離部5とが一体化した構造であっても構わない。また、搬送ラインL3、搬送路7、および搬送ライン4が一体化した構造であってもよい。 In the present embodiment, the desorption portion 4 and the separation portion 5 are described separately in order to explain in detail each step performed by the coating mist treatment apparatus 10, but the desorption portion 4 and the separation portion 5 are described separately. It may be a structure in which and is integrated. Further, the transport line L3, the transport path 7, and the transport line 4 may be integrated.
以下、上記で説明した塗装ミスト処理装置10を用いた実施例について説明する。 Hereinafter, an example using the coating mist processing apparatus 10 described above will be described.
<実施例1>
実施例1の塗料ミスト処理装置10では、粒子充填槽2には、フィルタ粒子1として、平均粒径(直径)2mmのアルミナ製フィルタ粒子と平均流径4mmのアルミナ製フィルタ粒子とを混合して使用し、塗料ミスト含有ガスの通風方向の厚みが20mmとなるように充填した。また、脱離部4はフィルタ粒子1を回旋させて塗料成分を脱離する構造とし、分離部5は、高風速ガスを導入して塗料成分を塗料回収部に収容する構造とした。
<Example 1>
In the paint mist treatment apparatus 10 of Example 1, in the particle filling tank 2, as filter particles 1, alumina filter particles having an average particle diameter (diameter) of 2 mm and alumina filter particles having an average flow diameter of 4 mm are mixed. It was used and filled so that the thickness of the paint mist-containing gas in the ventilation direction was 20 mm. Further, the desorption portion 4 has a structure in which the filter particles 1 are rotated to desorb the paint component, and the separation section 5 has a structure in which a high wind speed gas is introduced to accommodate the paint component in the paint recovery section.
上記のように構成した実施例1の塗料ミスト処理装置10に対して、アクリル樹脂系の塗料ミストを1.8g/min含んだ塗料ミスト含有ガス10m3/minを発生させ、粒子充填槽2に導入した。なお、実施例1で用いた塗料ミストの平均粒径は10〜100μmと推定される。 To the paint mist treatment apparatus 10 of Example 1 configured as described above, a paint mist-containing gas 10 m 3 / min containing 1.8 g / min of acrylic resin-based paint mist was generated in the particle filling tank 2. Introduced. The average particle size of the paint mist used in Example 1 is estimated to be 10 to 100 μm.
上記塗料ミスト含有ガスを導入した実施例1の塗料ミスト処理装置10について、塗料ミスト除去効率および圧力損失を測定した。塗料ミスト除去効率は、粒子充填槽2の入口ガスと出口ガスとをガラス濾紙に吸引し、塗料ミストを捕集し、その重量を測定し、透過率から求めた。また、圧力損失は、粒子充填槽2の入口ガスダクトと出口ガスダクトとの静圧を測定し、その差圧から求めた。 The paint mist removal efficiency and pressure loss of the paint mist treatment apparatus 10 of Example 1 into which the paint mist-containing gas was introduced were measured. The paint mist removal efficiency was determined by sucking the inlet gas and the outlet gas of the particle filling tank 2 into a glass filter paper, collecting the paint mist, measuring the weight thereof, and determining the transmittance. Further, the pressure loss was obtained by measuring the static pressure between the inlet gas duct and the outlet gas duct of the particle filling tank 2 and obtaining the differential pressure thereof.
結果、塗料ミスト処理装置10の稼動0.1時間後、2時間後、4時間後の塗料ミスト除去効率は99%、99%、99%であり、圧力損失は600、610、600Paであった。時間が経過しても圧力損失が安定していることから、実施例1の塗料ミスト処理装置10は、塗料成分の捕集、脱離、分離を安定して行えることがわかる。 As a result, the paint mist removal efficiency was 99%, 99%, 99% and the pressure loss was 600, 610, 600 Pa after 0.1 hour, 2 hours, and 4 hours of operation of the paint mist treatment apparatus 10. .. Since the pressure loss is stable over time, it can be seen that the paint mist treatment apparatus 10 of Example 1 can stably collect, desorb, and separate the paint components.
<実施例2>
実施例2の塗料ミスト処理装置10は、粒子充填槽2には、フィルタ粒子1として、平均粒径2mmのフィルタ粒子のみを使用した以外は、実施例1の塗料ミスト処理装置10と同構造とした。また、実施例2の塗料ミスト処理装置10に対して、導入した塗料ミスト含有ガスも導入条件も実施例1と同じにし、同じ操作、同じ測定を行った。
<Example 2>
The paint mist treatment device 10 of Example 2 has the same structure as the paint mist treatment device 10 of Example 1 except that only filter particles having an average particle size of 2 mm are used as the filter particles 1 in the particle filling tank 2. did. Further, for the paint mist treatment apparatus 10 of Example 2, the introduced paint mist-containing gas and the introduction conditions were the same as those of Example 1, and the same operation and the same measurement were performed.
実施例2では、塗料ミスト処理装置10の稼動0.1時間後、2時間後、4時間後の塗料ミスト除去効率は99%、99%、99%であり、圧力損失は650、740、730Paであった。圧力損失が稼働0.1後から2時間後で上昇する経時変化が確認され、その後も圧力損失の値が回復しなかった。このことから、実施例2では、塗料成分が一部フィルタ粒子1に残存していると考えられる。稼働4時間後で圧力損失は安定していることから、実施例2の塗装ミスト処理装置10は、塗料成分の一部は残存するが、安定して塗料成分の捕集、脱離、分離を行えることがわかる。 In the second embodiment, the paint mist removal efficiency after 0.1 hour, 2 hours, and 4 hours of operation of the paint mist treatment apparatus 10 is 99%, 99%, 99%, and the pressure loss is 650, 740, 730 Pa. Met. It was confirmed that the pressure loss increased over time 2 hours after the operation 0.1, and the pressure loss value did not recover even after that. From this, it is considered that in Example 2, a part of the paint component remains in the filter particles 1. Since the pressure loss is stable after 4 hours of operation, the coating mist treatment apparatus 10 of Example 2 stably collects, desorbs, and separates the coating component, although a part of the coating component remains. You can see that you can do it.
以上で説明した実施の形態および各実施例は、すべての点で例示であって、制限的なものではない。本発明の技術的範囲は、特許請求の範囲によって画定され、また特許請求の範囲の記載と均等の意味および範囲内でのすべての変更を含むものである。 The embodiments and examples described above are exemplary in all respects and are not restrictive. The technical scope of the present invention is defined by the scope of claims and includes all modifications within the meaning and scope equivalent to the description of the scope of claims.
1 フィルタ粒子
2 粒子充填槽
3 粒子排出部
4 脱離部
5 分離部
6 塗料回収部
7 循環路
8 塗料成分
9 凸凹部
10 塗料ミスト処理装置
L1〜L5 搬送ライン
1 Filter particle 2 Particle filling tank 3 Particle discharge part 4 Detachment part 5 Separation part 6 Paint recovery part 7 Circulation path 8 Paint component 9 Concavo-convex 10 Paint mist treatment device L1 to L5 Conveyance line
Claims (7)
前記塗料成分が付着したフィルタ粒子から該塗料成分を脱離する脱離部と、
前記粒子充填槽から前記離脱部へフィルタ粒子を排出させる粒子排出部と、
前記脱離部にて脱離された塗料成分とフィルタ粒子とを分離する分離部と、
前記分離部にて分離されたフィルタ粒子を再び前記粒子充填槽へ充填する循環路と、を備え、
前記脱離部は、塗料成分が付着したフィルタ粒子同士の衝突により、フィルタ粒子から塗料成分を脱離させ、
前記フィルタ粒子として、重量の異なる2種類以上のフィルタ粒子を使用し、
前記フィルタ粒子のうち質量の大きな粒子は、質量の小さな粒子が前記脱離部での脱離に必要なエネルギーが得られる程度混入されている、ことを特徴とする塗料ミスト処理装置。 The filter particles to which the paint component adheres are filled, and by introducing a paint mist-containing gas containing the paint mist composed of the paint component, the paint component is attached to the filter particles and removed, and the paint component is removed. A particle filling tank that discharges the processed gas and
A desorption portion that desorbs the paint component from the filter particles to which the paint component is attached,
A particle discharge part that discharges filter particles from the particle filling tank to the detachment part,
A separation part that separates the paint component and the filter particles that were desorbed at the desorption part,
A circulation path for refilling the particle filling tank with the filter particles separated by the separation portion is provided.
The detached portion desorbs the paint component from the filter particles by collision between the filter particles to which the paint component is attached.
As the filter particles, two or more types of filter particles having different weights are used.
A paint mist treatment apparatus, wherein particles having a large mass among the filter particles are mixed with particles having a small mass to such an extent that energy required for desorption at the desorption portion can be obtained .
前記塗料成分が付着したフィルタ粒子から該塗料成分を脱離する脱離工程と、
前記脱離工程にて脱離された塗料成分とフィルタ粒子とを分離する分離工程と、
前記分離工程にて分離されたフィルタ粒子を再び前記排出工程で用いるように循環させる循環工程と、
を含み、
前記脱離工程では、塗料成分が付着したフィルタ粒子同士を衝突させて、フィルタ粒子から塗料成分を脱離させ、
前記フィルタ粒子として、重量の異なる2種類以上のフィルタ粒子を使用し、
前記フィルタ粒子のうち質量の大きな粒子は、質量の小さな粒子が前記脱離部での脱離に必要なエネルギーが得られる程度混入されている、ことを特徴とする塗料ミスト処理方法。 A discharge step in which a paint mist-containing gas containing a paint mist composed of a paint component is brought into contact with the filter particles, the paint component is attached to the filter particles to be removed, and the treated gas from which the paint component has been removed is discharged.
A desorption step of desorbing the paint component from the filter particles to which the paint component is attached, and
A separation step of separating the paint component desorbed in the desorption step and the filter particles,
A circulation step in which the filter particles separated in the separation step are circulated again for use in the discharge step, and
Only including,
In the desorption step, the filter particles to which the paint component is attached are made to collide with each other to desorb the paint component from the filter particles.
Two or more types of filter particles having different weights are used as the filter particles.
A coating mist treatment method, wherein particles having a large mass among the filter particles are mixed with particles having a small mass to such an extent that energy required for desorption at the desorption portion can be obtained .
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