JP2006181503A - Treatment method and apparatus for coating-booth circulation water - Google Patents

Treatment method and apparatus for coating-booth circulation water Download PDF

Info

Publication number
JP2006181503A
JP2006181503A JP2004378911A JP2004378911A JP2006181503A JP 2006181503 A JP2006181503 A JP 2006181503A JP 2004378911 A JP2004378911 A JP 2004378911A JP 2004378911 A JP2004378911 A JP 2004378911A JP 2006181503 A JP2006181503 A JP 2006181503A
Authority
JP
Japan
Prior art keywords
circulating water
paint
booth
alkaline solution
coating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2004378911A
Other languages
Japanese (ja)
Inventor
Shigenori Kazama
重徳 風間
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.)
Nissan Motor Co Ltd
Original Assignee
Nissan Motor Co Ltd
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 Nissan Motor Co Ltd filed Critical Nissan Motor Co Ltd
Priority to JP2004378911A priority Critical patent/JP2006181503A/en
Publication of JP2006181503A publication Critical patent/JP2006181503A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B14/00Arrangements for collecting, re-using or eliminating excess spraying material
    • B05B14/40Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths
    • B05B14/46Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths by washing the air charged with excess material
    • B05B14/462Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths by washing the air charged with excess material and separating the excess material from the washing liquid, e.g. for recovery
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Removal Of Specific Substances (AREA)
  • Details Or Accessories Of Spraying Plant Or Apparatus (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a treatment method for coating-booth circulation water capable of easily separating and extracting a coating component from a coating-collecting circulation water even in a coating booth using a water-based coating. <P>SOLUTION: The treatment method of coating-booth circulation water has a step for adding an alkaline solution to coating-booth circulation water of the coating booth 1, a step for filtering circulation water to which the alkaline solution is added to separate a filtrate from the residue, a step for neutralizing the filtrate and a step for reusing a neutralized filtrate as the coating-collecting circulation water. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、塗装ブース循環水を処理する方法及び処理装置に関する。   The present invention relates to a method and a processing apparatus for processing paint booth circulating water.

中塗り塗装や上塗り塗装などのように塗装ガンによる噴霧塗装を行う塗装ブースにおいては、オーバースプレーした塗料を集約して処理するための処理装置が設けられている。従来の処理装置では、塗装ブース床のスノコ下にピットを設け、ブースの両側から水を流し続けることで、オーバースプレーした塗料をピットに捕集する(特許文献1の図3参照)。   In a painting booth that performs spray painting with a painting gun such as intermediate coating or top coating, a processing device is provided for collecting and processing oversprayed paint. In the conventional processing apparatus, a pit is provided under the slats of the painting booth floor, and water is continuously flowed from both sides of the booth, thereby collecting the oversprayed paint in the pit (see FIG. 3 of Patent Document 1).

ところで、塗料捕集用水を循環させることでオーバースプレーした塗料を捕集する場合、塗料が有機溶剤系塗料であるときには、分散剤や沈降剤としての界面活性剤を用いて循環水中に塗料を分散または沈降させることで捕集し、循環水から塗料を分離抽出したのち清浄な水を循環水として再利用するが、元来有機溶剤は水に溶けないので分離抽出処理は比較的容易に行うことができる。   By the way, when collecting oversprayed paint by circulating paint collecting water, when the paint is an organic solvent-based paint, the paint is dispersed in the circulating water using a surfactant as a dispersant or a settling agent. Or, it is collected by settling, and the paint is separated and extracted from the circulating water, and then clean water is reused as the circulating water. However, the organic solvent does not dissolve in water, so the separation and extraction process should be relatively easy. Can do.

しかしながら、近時多用されつつある水系塗料は循環水に溶解してしまうので、循環水を再利用する場合に塗料成分を分離抽出することは、有機溶剤系塗料に比べて困難である。   However, since water-based paints that are frequently used recently are dissolved in circulating water, it is difficult to separate and extract paint components when recycling water is used, compared to organic solvent-based paints.

たとえば、電着塗料の再生装置にも多用されている限外濾過装置(UF:高圧をかけて逆浸透膜により塗料成分を分離する装置)を用いれば循環水から塗料成分を分離抽出することは可能である(たとえば、特許文献2参照)が、限外濾過装置は高価で、しかもランニングコストも高いという欠点がある。電着塗料の再生装置に利用する場合は、電着塗料が同一であるために電着塗料を再生処理することができ、これがランニングコスト増を補って余りあるが、上塗り塗装ブースでは多様な塗料が使用されるので、塗料を再生することは現実的には困難であり、再生できるのは循環水のみである。多色の中塗り塗料を使用する中塗りブースについても同様の理由がある。したがって、限外濾過装置を塗装ブースの再生処理に使用するのは非現実的であった。
特開2000−93860号公報 特開平6−55134号公報
For example, if an ultrafiltration device (UF: a device that separates paint components with a reverse osmosis membrane by applying a high pressure) that is also widely used in an electrodeposition paint regeneration device, the paint components can be separated and extracted from the circulating water. Although it is possible (see, for example, Patent Document 2), the ultrafiltration device is disadvantageous in that it is expensive and the running cost is high. When used in an electrodeposition paint recycling device, the electrodeposition paint can be regenerated because the same electrodeposition paint, which compensates for the increase in running costs. Therefore, it is practically difficult to regenerate the paint, and only the circulating water can be regenerated. There is a similar reason for an intermediate coating booth that uses a multicolor intermediate coating. Therefore, it was unrealistic to use the ultrafiltration device for the regeneration process of the painting booth.
JP 2000-93860 A JP-A-6-55134

本発明は、水系塗料を使用する塗装ブースであっても塗料捕集用循環水から塗料成分を簡便に分離抽出することができる塗装ブース循環水の処理方法及び装置を提供することを目的とする。
上記目的を達成するために、本発明の塗装ブース循環水の処理方法は、塗装ブースの塗料捕集用循環水にアルカリ性溶液を添加するステップと、前記アルカリ性溶液が添加された循環水を濾過して濾液と残渣に分離するステップと、前記濾液を中和するステップと、前記中和された濾液を塗料捕集用循環水として再利用するステップとを有することを特徴とする。
An object of the present invention is to provide a processing method and apparatus for painting booth circulating water that can easily separate and extract coating components from circulating water for collecting paint even in a painting booth that uses water-based paint. .
In order to achieve the above object, the method for treating circulating water in a painting booth according to the present invention includes a step of adding an alkaline solution to circulating water for collecting paint in a painting booth, and filtering the circulating water to which the alkaline solution has been added. And separating the filtrate into a residue, neutralizing the filtrate, and reusing the neutralized filtrate as paint collection circulating water.

また、上記目的を達成するために、本発明の塗装ブース循環水の処理装置は、塗装ブースの塗料捕集用循環水にアルカリ性溶液を添加する手段と、前記アルカリ性溶液が添加された循環水を濾過して濾液と残渣に分離する手段と、前記濾液を中和する手段と、前記中和された濾液を塗装ブースに戻す手段と、を有することを特徴とする。   In order to achieve the above object, the coating booth circulating water treatment apparatus of the present invention comprises means for adding an alkaline solution to the coating booth for collecting paint in the coating booth, and circulating water to which the alkaline solution is added. It has a means to filter and isolate | separate into a filtrate and a residue, A means to neutralize the said filtrate, A means to return the said neutralized filtrate to a coating booth, It is characterized by the above-mentioned.

水を溶媒とする水系塗料にアルカリ性電解水などのアルカリ性溶液を加えるとゲル化する。これは、水系塗料は、樹脂成分を溶媒である水に分散させるためにカルボン酸などの酸性の極性基を有するが、これにアルカリ性溶液を加えると、それまで分散していた樹脂粒子が膨潤(ゲル化)するからである。本発明では、このことを利用し、塗料捕集用循環水にアルカリ性溶液を添加する。これにより、循環水中で塗料成分がゲル化するので、次の濾過処理によって容易に塗料成分と水成分とに分離することができる。濾過されて残渣となった塗料成分は、濃縮/乾燥などののち廃棄処分されるが、濾過された濾液は塗料成分が含まれない水であることから、酸性溶液によって中和したのち循環水として再利用することができる。   Gelation occurs when an alkaline solution such as alkaline electrolyzed water is added to an aqueous paint containing water as a solvent. This is because water-based paints have acidic polar groups such as carboxylic acid in order to disperse the resin component in water as a solvent, but when an alkaline solution is added thereto, the resin particles that have been dispersed so far swell ( This is because it gels. In the present invention, utilizing this, an alkaline solution is added to circulating water for collecting paint. Thereby, since a coating component gelatinizes in circulating water, it can isolate | separate into a coating component and a water component easily by the following filtration process. The paint component that has been filtered to form a residue is discarded after concentration / drying, but the filtered filtrate is water that does not contain the paint component. Can be reused.

本発明によれば、限外濾過装置などの高価な濾過装置ではなく簡便かつ廉価な濾過装置を用いて塗料成分と水とを分離することができ、また水を再生することができる。   According to the present invention, a paint component and water can be separated using a simple and inexpensive filtration device, not an expensive filtration device such as an ultrafiltration device, and water can be regenerated.

発明の実施の形態BEST MODE FOR CARRYING OUT THE INVENTION

以下、本発明の実施形態を図面に基づいて説明する。
図1は本実施形態に係る塗装ブースを示す断面図であり、中塗り塗装ブースや上塗り塗装ブースの何れにも適用することができる。特に、水系塗料を使用する塗装ブースに適用すると本発明の効果がより発揮される。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a cross-sectional view showing a coating booth according to the present embodiment, which can be applied to both an intermediate coating booth and a top coating booth. In particular, when applied to a painting booth using a water-based paint, the effect of the present invention is more exhibited.

同図に示すように、本実施形態に係る塗装ブース1は、トンネル状に形成されたパネル11と、ピット12とにより構成され、その内部の天井面13に天井フィルタが設けられ、床面14に簀の子(すのこ)が設けられている。これら天井フィルタが設けられた天井面13と簀の子が設けられた床面14との間が塗装室15を構成する。   As shown in the figure, the painting booth 1 according to the present embodiment is composed of a panel 11 formed in a tunnel shape and a pit 12, a ceiling filter is provided on the ceiling surface 13 inside thereof, and a floor surface 14. There is a child of the fox. A painting chamber 15 is formed between the ceiling surface 13 provided with the ceiling filter and the floor surface 14 provided with the ridge.

天井面13とパネルの天井との間には給気装置からの調和空気を案内する給気ダクト及び整流室16が設けられており、この整流室16にて整流された調和空気は天井フィルタを通過して塗装室15へ下向きに吹き出される。     An air supply duct for guiding conditioned air from the air supply device and a rectifying chamber 16 are provided between the ceiling surface 13 and the ceiling of the panel, and the conditioned air rectified in the rectifying chamber 16 has a ceiling filter. It passes through and is blown downward into the painting chamber 15.

床面14に設けられた簀の子の下のピット12は、オーバースプレーした塗料(飛散塗料)の捕集室17とされ、樋18からオーバーフローした水が捕集板19を流れる際にこの飛散塗料を補足してピット12に集約したのち、本発明に係る循環水処理装置へ送られる。これら樋18及び捕集板19は塗装ブース1の長手方向全域にわたって設けられており、塗装ブース1に被塗物が搬入されているときは常時樋18から循環水がオーバーフローして捕集板19をながれている。なお、同図では省略するが、この捕集室17には排気装置が設けられており、塗装室15を通過して捕集室17へ流下した調和空気は、熱回収されたのち系外へ排気される。     The pit 12 under the spider on the floor 14 is used as a collection chamber 17 for oversprayed paint (spatter paint). When the water overflowing from the spear 18 flows through the collection plate 19, this spatter paint is used. After supplementing and collecting in the pit 12, it is sent to the circulating water treatment apparatus according to the present invention. These troughs 18 and collecting plates 19 are provided over the entire length of the painting booth 1, and when the object to be coated is carried into the painting booth 1, the circulating water always overflows from the trough 18 and the collecting plates 19. It is flowing. Although not shown in the figure, the collection chamber 17 is provided with an exhaust device, and the conditioned air that has flowed into the collection chamber 17 after passing through the coating chamber 15 is recovered to the outside of the system. Exhausted.

同図において二点鎖線で示すBは、被塗物である自動車ボディであり、塗装台車に搭載された状態で、床面14に設けられたフロアコンベアにより塗装ブース内を定速度で搬送される。   B indicated by a two-dot chain line in the figure is an automobile body that is an object to be coated, and is transported at a constant speed in a painting booth by a floor conveyor provided on the floor 14 while being mounted on a painting carriage. .

本実施形態に係る循環水処理装置2は、塗装ブース1の捕集室17に捕集されたオーバースプレー塗料を含んだ循環水が導かれる第1のタンク21と、この第1のタンク21にアルカリ性溶液を添加するアルカリ性溶液添加装置22と、第1のタンク21にてアルカリ性溶液が添加された、塗料含有循環水を濾過する濾過装置23と、濾過装置23にて分離された濾液が導かれる第2のタンク24と、この第2のタンク24に中和剤を添加する中和剤添加装置25と、第2のタンク24にて中和された濾液を塗装ブース1の樋18に戻す配管26及びポンプ27と、を有する。   The circulating water treatment device 2 according to this embodiment includes a first tank 21 to which circulating water containing overspray paint collected in the collection chamber 17 of the painting booth 1 is guided, and the first tank 21. The alkaline solution addition device 22 for adding the alkaline solution, the filtration device 23 for filtering the paint-containing circulating water to which the alkaline solution has been added in the first tank 21, and the filtrate separated by the filtration device 23 are guided. A second tank 24, a neutralizer addition device 25 for adding a neutralizer to the second tank 24, and a pipe for returning the filtrate neutralized in the second tank 24 to the basket 18 of the painting booth 1. 26 and a pump 27.

第1のタンク21には、塗装ブース1の捕集室17に捕集された塗料含有循環水が、たとえばポンプなどを用いて定期的又は連続的に送られるが、この塗装ブース1にて使用される塗料が水系塗料だけでなく有機溶剤系塗料である場合には、塗装ブース1の捕集室17にて、またはこの第1のタンク21にて、分散剤又は沈降剤としての界面活性剤を添加し、有機溶剤系塗料の塗料成分及び溶剤成分が循環水の中で凝集するのを防止することが望ましい。   The paint-containing circulating water collected in the collection chamber 17 of the painting booth 1 is sent to the first tank 21 regularly or continuously using, for example, a pump. When the paint to be applied is not only a water-based paint but also an organic solvent-based paint, a surfactant as a dispersant or a settling agent in the collection chamber 17 of the painting booth 1 or in the first tank 21. It is desirable to prevent the paint component and the solvent component of the organic solvent-based paint from aggregating in the circulating water.

アルカリ性溶液添加装置22は、第1のタンク21に導かれた塗料含有循環水にアルカリ性溶液を添加するものであり、第1のタンク21に流入する塗料含有循環水の量に応じたアルカリ性溶液を供給する。これにより、循環水に含まれた水系塗料の塗料成分(樹脂成分)がゲル化する。すなわち、アルカリ性溶液を第1のタンク21に添加すると、循環水に溶解した水系塗料に含まれる酸性極性基、たとえばカルボキシル基COOHがアルカリ性溶液と結合し、これにより極性を失うので、それまで好適に分散していた塗料樹脂成分が膨潤し、その結果ゲル化する。   The alkaline solution addition device 22 adds an alkaline solution to the paint-containing circulating water guided to the first tank 21, and an alkaline solution corresponding to the amount of the paint-containing circulating water flowing into the first tank 21. Supply. As a result, the paint component (resin component) of the water-based paint contained in the circulating water is gelled. That is, when an alkaline solution is added to the first tank 21, an acidic polar group, for example, a carboxyl group COOH contained in a water-based paint dissolved in circulating water is combined with the alkaline solution, thereby losing the polarity. The dispersed coating resin component swells and gels as a result.

アルカリ性溶液としては、特に限定されないが、水酸化ナトリウムなどの強アルカリ溶液、水酸化アンモニウムまたは有機塩基を含有する水溶液、アルカリ性電解水を例示することができる。特に化学物質を含有しないので循環水の再利用の観点から、本例に係るアルカリ性水溶液としてアルカリ性電解水が最も好ましい。アルカリ性電解水をアルカリ性溶液に使用すると、水の電気分解の際に同時に生成される酸性電解水を後述する中和剤として利用することができ、pH調整も不要で、かつ酸性電解水を廃棄することもない。   Although it does not specifically limit as an alkaline solution, The aqueous solution containing ammonium hydroxide or an organic base, alkaline electrolyzed water, such as sodium hydroxide, can be illustrated. In particular, alkaline electrolyzed water is most preferable as the alkaline aqueous solution according to the present example from the viewpoint of recycling the circulating water because it does not contain chemical substances. When alkaline electrolyzed water is used for the alkaline solution, acidic electrolyzed water generated simultaneously with the electrolysis of water can be used as a neutralizing agent described later, pH adjustment is unnecessary, and acidic electrolyzed water is discarded. There is nothing.

また、ここで添加するアルカリ性溶液のpHは、8〜12であることが好ましい。pHが8未満であると本発明の効果が少なく、またpHが12を超えると中和剤の使用量やコストが増加することがある。   Moreover, it is preferable that the pH of the alkaline solution added here is 8-12. When the pH is less than 8, the effect of the present invention is small, and when the pH exceeds 12, the use amount and cost of the neutralizing agent may increase.

第1のタンク21にてアルカリ性溶液が添加された循環水は、濾過装置23に送られ、ここで濾液と残渣に分離される。本例の濾過装置23は、布フィルタ又はメッシュサイズが20〜100程度の粗いステンレスメッシュフィルタを用いた濾過装置であり、このフィルタによってゲル化した水系塗料成分と、界面活性剤にて分散又は沈降した有機溶剤系塗料成分が残渣として分離される。   The circulating water to which the alkaline solution is added in the first tank 21 is sent to the filtration device 23, where it is separated into a filtrate and a residue. The filtration device 23 of this example is a filtration device using a cloth filter or a coarse stainless mesh filter having a mesh size of about 20 to 100, and is dispersed or settled with a water-based paint component gelled by this filter and a surfactant. The organic solvent-based paint component is separated as a residue.

分離された残渣は、種々の顔料が無作為に混合してなるので塗料として再生することは困難である。したがって、集約した残渣を濃縮し乾燥したのち、廃棄処理する。   The separated residue is difficult to regenerate as a paint because various pigments are randomly mixed. Therefore, the aggregated residue is concentrated and dried, and then discarded.

濾過装置23を通過した濾液には、水系塗料成分及び有機溶剤系塗料成分は殆ど含まれていないが、アルカリ性溶液を添加したことによりpHが8〜11の中〜強アルカリ性溶液となっている。これをそのまま塗装ブース1の循環水として再利用すると、捕集室17内に塗料成分が沈着し、その除去作業が困難になる等の問題があることから、第2のタンク24に一旦集約し、中和剤添加装置25により中和剤を添加して中和する。中和剤としては、特に限定されず、塩酸や硫酸などの強酸などを用いることができるが、既述したように酸性電解水を用いることで、安全性や排水処理性が著しく高くなる。なお、この第2のタンク24における中和は厳密な意味での中和ではなく、上述した問題が生じない程度の範囲でpHを7近傍に調整する程度のものでよい。   The filtrate that has passed through the filtration device 23 contains almost no water-based paint component and no organic solvent-based paint component, but has become a medium to strong alkaline solution having a pH of 8 to 11 by adding an alkaline solution. If this is reused as circulating water in the painting booth 1 as it is, there is a problem that paint components are deposited in the collection chamber 17 and the removal operation becomes difficult. Then, the neutralizer is added by the neutralizer addition device 25 for neutralization. The neutralizing agent is not particularly limited, and a strong acid such as hydrochloric acid or sulfuric acid can be used. However, as described above, the use of acidic electrolyzed water significantly increases safety and wastewater treatment. The neutralization in the second tank 24 is not a strict meaning neutralization, but may be such that the pH is adjusted to around 7 within a range in which the above-described problem does not occur.

第2のタンク24にて中和された濾液は、ポンプ27によって吸引され、配管26を介して塗装ブース1の樋18に戻される。   The filtrate neutralized in the second tank 24 is sucked by the pump 27 and returned to the basket 18 of the painting booth 1 through the pipe 26.

以上のとおり、本実施形態に係る循環水の処理方法及び処理装置によれば、布フィルタ又はステンレスフィルタといった簡便な濾過装置のみを用いることにより、循環水に溶解した水系塗料成分を分離することができ、そして、濾液たる循環水を再利用することができる。特に、アルカリ性溶液としてアルカリ性電解水を用い、中和剤として酸性電解水を用いると、取り扱い上の安全性が著しく向上し、また時間が経てば普通の水に戻るので後処理等の必要もない。   As described above, according to the circulating water treatment method and treatment apparatus according to the present embodiment, the water-based paint component dissolved in the circulating water can be separated by using only a simple filtration device such as a cloth filter or a stainless steel filter. The circulating water as the filtrate can be reused. In particular, when alkaline electrolyzed water is used as the alkaline solution and acidic electrolyzed water is used as the neutralizing agent, the safety in handling is remarkably improved, and since it returns to normal water over time, there is no need for post-treatment. .

なお、以上説明した実施形態は、本発明の理解を容易にするために記載されたものであって、本発明を限定するために記載されたものではない。したがって、上記の実施形態に開示された各要素は、本発明の技術的範囲に属する全ての設計変更や均等物をも含む趣旨である。   The embodiment described above is described for facilitating the understanding of the present invention, and is not described for limiting the present invention. Therefore, each element disclosed in the above embodiment is intended to include all design changes and equivalents belonging to the technical scope of the present invention.

本発明の実施形態に係る循環水の処理装置を塗装ブースに適用した一例を示す断面図である。It is sectional drawing which shows an example which applied the processing apparatus for circulating water which concerns on embodiment of this invention to the painting booth.

符号の説明Explanation of symbols

1…塗装ブース
11…パネル
12…ピット
13…天井面
14…床面
15…塗装室
16…整流室
17…捕集室
18…樋
19…捕集板
2…循環水の処理装置
21…第1のタンク
22…アルカリ性溶液添加装置
23…濾過装置
24…第2のタンク
25…中和剤添加装置
26…配管
27…ポンプ

DESCRIPTION OF SYMBOLS 1 ... Painting booth 11 ... Panel 12 ... Pit 13 ... Ceiling surface 14 ... Floor 15 ... Painting room 16 ... Rectification room 17 ... Collection room 18 ... Trap 19 ... Collection board 2 ... Circulating water processing apparatus 21 ... 1st Tank 22 ... Alkaline solution addition device 23 ... Filtration device 24 ... Second tank 25 ... Neutralizer addition device 26 ... Pipe 27 ... Pump

Claims (10)

塗装ブースの塗料捕集用循環水にアルカリ性溶液を添加するステップと、前記アルカリ性溶液が添加された循環水を濾過して濾液と残渣に分離するステップと、前記濾液を中和するステップと、前記中和された濾液を塗料捕集用循環水として再利用するステップとを有する塗装ブース循環水の処理方法。 Adding an alkaline solution to circulating water for collecting paint in a paint booth; filtering the circulating water to which the alkaline solution has been added; separating the filtrate and residue; neutralizing the filtrate; and And recycling the neutralized filtrate as paint collecting circulating water. 前記アルカリ性溶液は、アルカリ性電解水を主成分とすることを特徴とする請求項1記載の塗装ブース循環水の処理方法。 2. The coating booth circulating water treatment method according to claim 1, wherein the alkaline solution contains alkaline electrolyzed water as a main component. 前記アルカリ性溶液のpHは、8〜12であることを特徴とする請求項1または2記載の塗装ブース循環水の処理方法。 The method of treating painting booth circulating water according to claim 1 or 2, wherein the alkaline solution has a pH of 8 to 12. 前記濾液を中和するステップにおいて、酸性電解水を主成分とする中和剤を用いることを特徴とする請求項2または3記載の塗装ブース循環水の処理方法。 4. The method for treating circulating water in a coating booth according to claim 2, wherein a neutralizing agent mainly composed of acidic electrolyzed water is used in the step of neutralizing the filtrate. 前記残渣は、濃縮処理及び/又は乾燥処理したのち廃棄処理されることを特徴とする請求項1〜4の何れかに記載の塗装ブース循環水の処理方法。 The said residue is a disposal process after a concentration process and / or a drying process, The processing method of the coating booth circulating water in any one of Claims 1-4 characterized by the above-mentioned. 塗装ブースの塗料捕集用循環水にアルカリ性溶液を添加する手段と、前記アルカリ性溶液が添加された循環水を濾過して濾液と残渣に分離する手段と、前記濾液を中和する手段と、前記中和された濾液を塗装ブースに戻す手段と、を有する塗装ブース循環水の処理装置。 Means for adding an alkaline solution to circulating water for collecting paint in a paint booth; means for filtering the circulating water to which the alkaline solution has been added to separate it into a filtrate and residue; means for neutralizing the filtrate; Means for returning the neutralized filtrate to the paint booth, and a paint booth circulating water treatment device. 前記アルカリ性溶液は、アルカリ性電解水を主成分とすることを特徴とする請求項6記載の塗装ブース循環水の処理装置。 The coating booth circulating water treatment apparatus according to claim 6, wherein the alkaline solution contains alkaline electrolyzed water as a main component. 前記アルカリ性溶液のpHは、8〜12であることを特徴とする請求項6または7記載の塗装ブース循環水の処理装置。 8. The coating booth circulating water treatment apparatus according to claim 6 or 7, wherein the pH of the alkaline solution is 8-12. 前記濾液を中和する手段は、酸性電解水を主成分とする中和剤を用いることを特徴とする請求項7または8記載の塗装ブース循環水の処理装置。 9. The processing apparatus for circulating paint booth water according to claim 7 or 8, wherein the means for neutralizing the filtrate uses a neutralizing agent mainly composed of acidic electrolyzed water. 前記残渣を濃縮処理及び/又は乾燥処理する手段を有することを特徴とする請求項6〜9の何れかに記載の塗装ブース循環水の処理装置。

The processing apparatus for circulating the coating booth according to any one of claims 6 to 9, further comprising means for concentrating and / or drying the residue.

JP2004378911A 2004-12-28 2004-12-28 Treatment method and apparatus for coating-booth circulation water Pending JP2006181503A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004378911A JP2006181503A (en) 2004-12-28 2004-12-28 Treatment method and apparatus for coating-booth circulation water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004378911A JP2006181503A (en) 2004-12-28 2004-12-28 Treatment method and apparatus for coating-booth circulation water

Publications (1)

Publication Number Publication Date
JP2006181503A true JP2006181503A (en) 2006-07-13

Family

ID=36734990

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004378911A Pending JP2006181503A (en) 2004-12-28 2004-12-28 Treatment method and apparatus for coating-booth circulation water

Country Status (1)

Country Link
JP (1) JP2006181503A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010046613A (en) * 2008-08-22 2010-03-04 Omega:Kk Scrubber mechanism
JP2012120935A (en) * 2010-12-06 2012-06-28 Uv Technica:Kk Method and device for treating circulation water of coating booth
WO2013008350A1 (en) 2011-07-08 2013-01-17 株式会社 ユーブイ・テクニカ Coating material spray mist treatment method
WO2013140653A1 (en) * 2012-03-23 2013-09-26 Kurushima Takeo Method for treating discharge gas
JP2019111481A (en) * 2017-12-22 2019-07-11 房総車体有限会社 Splash recovery system
CN115178543A (en) * 2022-07-22 2022-10-14 东风柳州汽车有限公司 Cleaning method for water-based paint conveying system
KR102675579B1 (en) * 2023-06-30 2024-06-13 김현진 Device for painting metal material surface

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010046613A (en) * 2008-08-22 2010-03-04 Omega:Kk Scrubber mechanism
JP2012120935A (en) * 2010-12-06 2012-06-28 Uv Technica:Kk Method and device for treating circulation water of coating booth
KR20140048964A (en) 2011-07-08 2014-04-24 가부시키가이샤 유브이?테크니카 Coating material spray mist treatment method
JP5286580B2 (en) * 2011-07-08 2013-09-11 株式会社 ユーブイ・テクニカ Treatment method of paint spray mist
CN103648661A (en) * 2011-07-08 2014-03-19 优威泰克株式会社 Coating material spray mist treatment method
WO2013008350A1 (en) 2011-07-08 2013-01-17 株式会社 ユーブイ・テクニカ Coating material spray mist treatment method
US9260624B2 (en) 2011-07-08 2016-02-16 UV Tech Co. Ltd. Coating material spray mist treatment method
KR101635288B1 (en) * 2011-07-08 2016-07-08 가부시키가이샤 유브이·테크니카 Coating material spray mist treatment method
WO2013140653A1 (en) * 2012-03-23 2013-09-26 Kurushima Takeo Method for treating discharge gas
JPWO2013140653A1 (en) * 2012-03-23 2015-08-03 武男 久留嶋 Exhaust gas treatment method
JP2019111481A (en) * 2017-12-22 2019-07-11 房総車体有限会社 Splash recovery system
CN115178543A (en) * 2022-07-22 2022-10-14 东风柳州汽车有限公司 Cleaning method for water-based paint conveying system
CN115178543B (en) * 2022-07-22 2023-08-18 东风柳州汽车有限公司 Cleaning method of water-based paint conveying system
KR102675579B1 (en) * 2023-06-30 2024-06-13 김현진 Device for painting metal material surface

Similar Documents

Publication Publication Date Title
KR102265310B1 (en) Methods and compositions for the treatment and recovery of purge solvent
JPS63294959A (en) Method and apparatus for purifying waste gas from paint or lacquer spray painting booth
JP2012120935A (en) Method and device for treating circulation water of coating booth
JP2006181503A (en) Treatment method and apparatus for coating-booth circulation water
CA2492183A1 (en) Method and device for recycling metal pickling baths
CN105457435A (en) Dry UV paint mist recycling and purifying system
US5393390A (en) Treatment and recycling of overspray from the spray application of waterborne coatings
JPH09506908A (en) Treatment and reuse of overspray from spray application of waterborne paints
JP5535967B2 (en) Vehicle washing system
JP2005125273A (en) Treating method and device of over-spray coating
EP0755723A2 (en) Spray booth paint reclamation apparatus and method
WO2019163251A1 (en) Electrodeposition coating facility
US20160144315A1 (en) Method and device for purifying exhaust air produced during wood processing
JP6001501B2 (en) Water-based uncoated paint recovery device and recovery method
JP2001170550A (en) Method of recycling water-based coating
CN214736160U (en) Ticket clip assembly line equipment
CN107626498A (en) A kind of water paint recycling paint finishing
EP0583314B1 (en) Treatment and recycling of overspray from the spray application of waterborne coatings
JP2002248386A (en) Method of recovering and recycling water paint
JPH02218463A (en) Coating equipment
JP2007050361A (en) Nonionic organic substance recovery method
CA2124554A1 (en) Method of removing paint
CN108579304A (en) Paint spray booth&#39;s purification system and purification method
US20030226807A1 (en) Method and apparatus for treating aqueous process baths and their associated waste streams
JPH07968A (en) Method for purifying filtrate of recovered paint