JP6120470B2 - Wet paint booth circulating water treatment agent and treatment method - Google Patents
Wet paint booth circulating water treatment agent and treatment method Download PDFInfo
- Publication number
- JP6120470B2 JP6120470B2 JP2016509606A JP2016509606A JP6120470B2 JP 6120470 B2 JP6120470 B2 JP 6120470B2 JP 2016509606 A JP2016509606 A JP 2016509606A JP 2016509606 A JP2016509606 A JP 2016509606A JP 6120470 B2 JP6120470 B2 JP 6120470B2
- Authority
- JP
- Japan
- Prior art keywords
- circulating water
- paint
- booth circulating
- booth
- water
- 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.)
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Images
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N37/00—Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom having three bonds to hetero atoms with at the most two bonds to halogen, e.g. carboxylic acids
- A01N37/52—Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom having three bonds to hetero atoms with at the most two bonds to halogen, e.g. carboxylic acids containing groups, e.g. carboxylic acid amidines
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/14—Paint wastes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/02—Odour removal or prevention of malodour
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- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
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- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
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Description
本発明は、湿式塗装ブース循環水の処理剤及び処理方法に関する。更に詳しくは、湿式塗装ブース循環水の悪臭防止及び清澄化に優れた効果を示す、特定のα−クロロベンズアルドキシム化合物を含有する湿式塗装ブース循環水の処理剤及び処理方法に関する。 The present invention relates to a treatment agent and a treatment method for circulating water in a wet paint booth. More specifically, the present invention relates to a treatment agent and a treatment method for wet paint booth circulating water containing a specific α-chlorobenzaldoxime compound, which exhibits an excellent effect in preventing bad smell and clarification of the wet paint booth circulating water.
従来、自動車や電気製品等の塗装法の一種として、塗料を被塗装物に噴霧するスプレー塗装法がある。スプレー塗装法では塗料品質の保持及び作業環境の保全のため、湿式塗装ブース内で塗料の噴霧が行われている。 2. Description of the Related Art Conventionally, there is a spray coating method in which paint is sprayed on an object to be coated as a kind of coating method for automobiles, electrical products and the like. In the spray painting method, paint is sprayed in a wet painting booth in order to maintain the quality of the paint and preserve the work environment.
この湿式塗装ブースは、被塗装物に塗料を噴霧するための塗装室と、塗装室の空気を吸引するためのファンを有するダクトと、吸引した空気とブース循環水とを接触させるための接触部と、ブース循環水を貯留可能なピットとが備えられている。この湿式塗装ブースでは、被塗装物に塗着しなかった未塗着塗料がファンによって空気とともにダクト内に吸引される。この際、未塗着塗料は接触部においてブース循環水と接触して捕集され、未塗着塗料を沈殿あるいは浮上させることにより分離される。こうして分離された未塗着塗料は回収され、廃棄処分される。 This wet painting booth has a painting chamber for spraying paint on an object to be coated, a duct having a fan for sucking air in the painting chamber, and a contact portion for bringing the sucked air and the booth circulating water into contact with each other. And a pit capable of storing booth circulating water. In this wet painting booth, uncoated paint that has not been applied to the object to be coated is sucked into the duct together with air by the fan. At this time, the uncoated paint is collected in contact with the booth circulating water at the contact portion, and separated by settling or floating the uncoated paint. The uncoated paint thus separated is collected and discarded.
しかし、未塗着塗料の一部は分離されることなくブース循環水中に浮遊して循環し、配管内面等に付着してブース循環水の循環水量を低下させる。さらに、その循環水量の低下が著しい場合には、塗装作業を停止しなければならないことさえある。こうした不具合を防止するため、ブース循環水にあらかじめ塗料処理剤を添加しておき、ブース循環水内に浮遊する未塗着塗料を不粘着化するとともに固液分離を容易にすることが行われている。 However, a portion of the unpainted paint floats and circulates in the booth circulating water without being separated, and adheres to the inner surface of the piping and reduces the circulating water volume of the booth circulating water. Furthermore, the painting operation may even need to be stopped if the amount of circulating water is significantly reduced. In order to prevent such problems, a paint treatment agent is added to the booth circulating water in advance to detack the unpainted paint floating in the booth circulating water and facilitate solid-liquid separation. Yes.
このような塗料処理剤として、油性塗料に関して、例えば苛性ソーダ等のアルカリ剤、カチオン性ポリマー、無機凝集剤、メラミン−アルデヒド樹脂酸コロイド(特許文献1参照)等が挙げられる。アルカリ剤は未塗着油性塗料の表面をケン化し、不粘着化することによって、配管への未塗着油性塗料の付着を防ぐものである。また、カチオン性ポリマー、無機凝集剤及びメラミン−アルデヒド樹脂酸コロイドは、未塗着塗料の表面に付着し、不粘着化して固液分離を容易化するものである。
また、未塗着水性塗料に対しては、ポリエチレンイミンを成分として含む塗料処理剤(特許文献2参照)や、カチオン性有機化合物とアニオン性有機化合物とを含む塗料処理剤(特許文献3参照)等が用いられている。これらの塗料処理剤は、ブース循環水中に均一に分散あるいは溶解した未塗着水性塗料の固液分離を容易にするものである。Examples of such paint treating agents include, for oil-based paints, alkaline agents such as caustic soda, cationic polymers, inorganic flocculants, melamine-aldehyde resin acid colloids (see Patent Document 1), and the like. The alkaline agent saponifies the surface of the uncoated oil-based paint to make it non-tacky, thereby preventing the non-coated oil-based paint from adhering to the pipe. Further, the cationic polymer, the inorganic flocculant and the melamine-aldehyde resin acid colloid adhere to the surface of the uncoated paint and become non-tacky to facilitate solid-liquid separation.
For uncoated water-based paints, a paint treatment agent containing polyethyleneimine as a component (see Patent Document 2) or a paint treatment agent containing a cationic organic compound and an anionic organic compound (see Patent Document 3). Etc. are used. These paint treatment agents facilitate solid-liquid separation of uncoated water-based paints that are uniformly dispersed or dissolved in Booth circulating water.
このように、従来のブース循環水の処理方法では、ブース循環水中の未塗着塗料の種類に応じた、適切な塗料処理剤を選択することにより、未塗着塗料の固液分離を容易に行うことができる。しかし、近年では、環境目標として産廃排出量削減、リサイクル推進を進める企業が増え、ブース循環水についても水入れ替え頻度の減少、長期に渡る繰り返し使用が行われ、そのため、ブース循環水の汚染度は高まり、濁質成分が濃縮する傾向にある。また、有機溶剤の環境への影響を考慮して、従来から多用されている油性塗料の他、水性塗料の使用も大幅に増加し、その結果、油性塗料単独の塗装ブース、水性塗料単独の塗装ブース、更に水性塗料と油性塗料の混合使用の塗装ブースなど、塗装ブースの運転形式は複雑で多様になってきており、それに伴い、ブース循環水に溶解もしくは分散する塗料成分や溶剤成分もますます複雑化し、かつ増加しているため、この状況に起因する新たな諸問題が発生してきた。 As described above, in the conventional booth circulating water treatment method, solid-liquid separation of uncoated paint is facilitated by selecting an appropriate paint treatment agent according to the type of uncoated paint in the booth circulating water. It can be carried out. However, in recent years, the number of companies promoting industrial waste reduction and recycling promotion as environmental targets has increased, and the frequency of replacement of booth circulating water has been reduced, and repeated use over a long period of time. It tends to increase and concentrate turbid components. Considering the environmental impact of organic solvents, the use of water-based paints as well as oil-based paints that have been widely used in the past has greatly increased. The operating system of the painting booth, such as a booth and a painting booth that uses a mixture of water-based paint and oil-based paint, has become complex and diverse, and along with that, paint components and solvent components that dissolve or disperse in the booth circulating water are also increasing Because of increasing complexity and increasing, new problems have arisen due to this situation.
このような新たな問題の第一が悪臭の深刻化であり、第二が濁質成分の高濃度化である。水性塗料の使用の増加に伴って、前記の通り、ブース循環水に溶解もしくは分散する塗料成分や溶剤成分もますます複雑化し、かつ増加しているため、ブース循環水のCODは飛躍的に増加しており、油性塗料を使用していた従来の有機溶剤臭を主とする悪臭とは全く異なる複雑で深刻な様相を呈している。また、ブース循環水の濁質成分の濃縮及び増加は、チョウバエやユスリカなどの害虫の発生を促し、作業環境の悪化ならび塗装不良の増加をもたらす。さらには、水中の濁質成分が沈降すると、清掃時の産廃処理量が増加し清掃費用がかかることになる。また、高濃度の濁質成分を有するブース循環水は悪臭を生じやすく作業環境ならびに周辺環境の悪化ももたらす。 The first of such new problems is the worsening of bad odor, and the second is the increase in the concentration of turbid components. As the use of water-based paints increases, as mentioned above, the paint components and solvent components that dissolve or disperse in the booth circulating water are becoming more complex and increasing, so the COD of the booth circulating water increases dramatically. Therefore, it has a complicated and serious aspect that is completely different from the conventional bad odor mainly of organic solvent odor that uses oil-based paint. In addition, the concentration and increase of turbid components in the booth circulation water promote the generation of insect pests such as butterflies and chironomids, leading to deterioration of the working environment and an increase in painting defects. Furthermore, when the turbid component in water settles, the amount of industrial waste processing at the time of cleaning increases, and cleaning costs are required. In addition, booth circulating water having a high concentration of turbid components is liable to produce malodors and causes deterioration of the working environment and the surrounding environment.
従来より、油性塗料中に含まれる有機溶剤して多量に使用されるトルエン、キシレン、酢酸エチル及びメチルイソブチルケトンなどが、ブース循環水に混入、溶解して、有機溶剤臭、アルデヒド臭、カルボン酸臭等を発生させ、その結果、作業環境の悪化を招き周辺住民からの苦情の原因にもなっていた。その対策として、殺菌剤である、ヘキサヒドロ−1,3,5−トリス(2−ヒドロキシエチル)−S−トリアジンを含有する塗料処理剤(特許文献4参照)やテトラアルキルホスホニウム塩を含有する塗料処理剤(特許文献5参照)が提案されており、また、オゾンの使用(特許文献6参照)などが提案されている。 Conventionally, toluene, xylene, ethyl acetate and methyl isobutyl ketone, which are used in large quantities as organic solvents in oil-based paints, are mixed and dissolved in booth circulating water, resulting in organic solvent odor, aldehyde odor, carboxylic acid Odors were generated, resulting in a worsening work environment and causing complaints from the surrounding residents. As a countermeasure, a paint treatment agent containing hexahydro-1,3,5-tris (2-hydroxyethyl) -S-triazine as a bactericidal agent (see Patent Document 4) or a paint treatment containing a tetraalkylphosphonium salt. An agent (see Patent Document 5) has been proposed, and the use of ozone (see Patent Document 6) has been proposed.
しかしながら、上記のような近年の水性塗料の大幅な使用増加と塗装ブースの運転形式の複雑化、多様化に対しては、従来の主に油性塗料を対象とした悪臭対策では効果が不十分であり、また、高濃度の濁質成分の除去についても効果的な対策が得られていない。 However, in order to deal with the significant increase in the use of water-based paints in recent years and the complexity and diversification of the operating system of painting booths, the effects of conventional measures against bad odor mainly for oil-based paints are not sufficient. In addition, no effective countermeasures have been obtained for the removal of high-concentration turbid components.
本発明は、上記従来の実情に鑑みてなされたものであり、近年の水性塗料の大幅な使用増加と塗装ブースの運転形式の複雑化、多様化の状況において発生している悪臭の深刻化や濁質成分の高濃度化に対応できる湿式塗装ブース処理剤及び処理方法を提供することを解決すべき課題としている。 The present invention has been made in view of the above-mentioned conventional circumstances, and the recent significant increase in the use of water-based paints, the complexity of the operation mode of paint booths, It is an object to be solved to provide a wet coating booth treatment agent and a treatment method that can cope with a high concentration of turbid components.
本発明者らは、上記課題を解決すべく、鋭意研究の結果、特定のα−クロロベンズアルドキシム化合物が湿式塗装ブース循環水の悪臭を防止する優れた効果を有することに加えて、更に湿式塗装ブース循環水の濁質成分を除去して清澄化する効果をも有することを見出し、また、この特定のα−クロロベンズアルドキシム化合物は、油性塗料単独、水性塗料単独及び水性塗料と油性塗料の混合使用の、運転形式の異なる塗装ブースにおいても、安定して前記の効果を発揮できることも確認して本発明を完成するに至った。 In order to solve the above-mentioned problems, the present inventors have intensively studied, and as a result, the specific α-chlorobenzaldoxime compound has an excellent effect of preventing the bad odor of the wet paint booth circulating water, and further wet. The paint booth has also been found to have the effect of removing turbid components from circulating water and clarifying, and this specific α-chlorobenzaldoxime compound is used in oil paints alone, water paints alone, water paints and oil paints. The present invention has been completed by confirming that the above-mentioned effects can be stably exhibited even in coating booths of different operation modes that are mixed and used.
α−クロロベンズアルドキシム化合物は一般的に水系の殺菌剤として用いられるため、本発明者らは、本発明で用いられる特定のα−クロロベンズアルドキシム化合物の、油性塗料単独使用条件下での悪臭防止効果は予想できたが、水性塗料単独使用条件下及び水性塗料と油性塗料の混合使用条件下でも安定した悪臭防止効果が得られ、更に、いずれの条件下においても、ブース循環水の濁質成分を除去して清澄化する効果をも発揮することは予想もできないことであった。 Since α-chlorobenzaldoxime compounds are generally used as water-based disinfectants, the present inventors have determined that specific α-chlorobenzaldoxime compounds used in the present invention can be used under the condition of using an oil-based paint alone. Although the odor prevention effect could be expected, a stable odor prevention effect was obtained even under the condition of using a water-based paint alone and under the condition of using a mixture of a water-based paint and an oil-based paint. It was impossible to predict the effect of clarifying by removing the quality component.
すなわち、本願発明は、下記一般式(1)で表されるα−クロロベンズアルドキシム化合物を含有することを特徴とする湿式塗装ブース循環水処理剤に関するものである。
本願発明は、前記一般式(1)で表される化合物が、α−クロロ−p−クロロベンズアルドキシムである湿式塗装ブース循環水処理剤を提供するものである。 The present invention provides a wet paint booth circulating water treatment agent in which the compound represented by the general formula (1) is α-chloro-p-chlorobenzaldoxime.
本願発明は、下記一般式(1)で表されるα−クロロベンズアルドキシム化合物を、湿式塗装ブース循環水に添加することを特徴とする湿式塗装ブース循環水処理方法に関するものである。
本願発明は、前記一般式(1)で表されるα−クロロベンズアルドキシム化合物を、湿式塗装ブース循環水中の濃度が、0.1〜100mg/Lとなるように添加することを特徴とする湿式塗装ブース循環水処理方法を提供するものである。 The present invention is characterized in that the α-chlorobenzaldoxime compound represented by the general formula (1) is added so that the concentration in the wet coating booth circulating water is 0.1 to 100 mg / L. A wet paint booth circulating water treatment method is provided.
本願発明は、また、前記一般式(1)で表されるα−クロロベンズアルドキシム化合物が、α−クロロ−p−クロロベンズアルドキシムである湿式塗装ブース循環水処理方法を提供するものである。 The present invention also provides a wet paint booth circulating water treatment method in which the α-chlorobenzaldoxime compound represented by the general formula (1) is α-chloro-p-chlorobenzaldoxime. .
本発明の湿式塗装ブース循環水処理剤及び処理方法の適用によって、使用する塗料の種類に関係なく、ブース循環水の悪臭防止と清澄化の優れた効果を得ることができる。 By applying the wet paint booth circulating water treatment agent and the treatment method of the present invention, it is possible to obtain excellent effects of preventing bad smell and clarifying of booth circulating water regardless of the type of paint used.
本発明の湿式塗装ブース循環水処理剤及び処理方法が処理対象とする湿式塗装ブースの形式には特に制限はなく、ウォーターカーテン式、ベンチュリー式、ノーポンプ式及びこれらの形式の変形形式、並びにこれらの形式の塗装ブースに各種付帯設備を接続した塗装ブースも含まれる。 There are no particular restrictions on the type of wet coating booth to be treated by the wet coating booth circulating water treatment agent and processing method of the present invention, water curtain type, venturi type, no pump type and variations of these types, as well as these types It also includes a painting booth where various incidental facilities are connected to the painting booth.
本発明の湿式塗装ブース循環水処理剤及び処理方法において、処理の対象となる油性塗料は、特に限定はなく、例えばエポキシ樹脂塗料、ポリエステル樹脂塗料、ウレタン樹脂塗料、アルキド樹脂塗料、アミノ樹脂塗料、ビニル樹脂塗料、アクリル樹脂塗料、フェノール樹脂塗料、セルロース誘導体塗料、酒精塗料等が挙げられる。また、処理の対象となる水性塗料も、特に限定はなく、例えば水性アルキッド樹脂塗料、水性ポリエステル樹脂塗料、水性アクリル樹脂塗料、水性ポリウレタン樹脂塗料等が挙げられる。 In the wet paint booth circulating water treatment agent and treatment method of the present invention, the oil-based paint to be treated is not particularly limited. For example, epoxy resin paint, polyester resin paint, urethane resin paint, alkyd resin paint, amino resin paint, Examples include vinyl resin paints, acrylic resin paints, phenol resin paints, cellulose derivative paints, and alcoholic paints. Also, the water-based paint to be treated is not particularly limited, and examples thereof include a water-based alkyd resin paint, a water-based polyester resin paint, a water-based acrylic resin paint, and a water-based polyurethane resin paint.
本発明の湿式塗装ブース循環水処理剤及び処理方法が処理対象とする湿式塗装ブースでの塗料の使用形態には特に制限はなく、油性塗料単独使用、水性塗料単独使用及び水性塗料と油性塗料の混合使用のいずれの使用形態のブースであっても適用できる。 There is no particular limitation on the usage form of the paint in the wet paint booth to be treated by the wet paint booth circulating water treatment agent and treatment method of the present invention, the oil paint alone use, the water paint alone use, and the water paint and oil paint The present invention can be applied to any use booth of mixed use.
本発明の湿式塗装ブース循環水処理剤及び処理方法に用いられる特定のα−クロロベンズアルドキシム化合物としては、例えば、α−クロロベンズアルドキシム、α−クロロ−p−クロロベンズアルドキシム、α−クロロ−ベンズアルドキシムアセテート、及びα−クロロ−p−クロロベンズアルドキシムアセテート等が挙げられ、中でもα−クロロ−p−クロロベンズアルドキシムが清澄化効果の点で好適である。 Specific α-chlorobenzaldoxime compounds used in the wet paint booth circulating water treatment agent and treatment method of the present invention include, for example, α-chlorobenzaldoxime, α-chloro-p-chlorobenzaldoxime, α- Examples include chloro-benzaldoxime acetate and α-chloro-p-chlorobenzaldoxime acetate. Among them, α-chloro-p-chlorobenzaldoxime is preferable in terms of the clarification effect.
本発明の湿式塗装ブース循環水処理剤は、有効成分である特定のα−クロロベンズアルドキシム化合物が水に難溶性であるため、親水性溶媒に溶解して調製する溶液の形態、又は微粒子にして水に分散させて調製する分散剤の形態となる。親水性溶媒としては、メタノール、エタノールなどのアルコール類、エチレングリコール、プロピレングリコール、ジエチレングリコール、ジプロピレングリコール等のグリコール類、メチルセロソルブ、フェニルセロソルブ、ジエチレングリコールモノメチルエーテル、ジプロピレングリコールモノエチルエーテル、トリプロピレングリコールモノメチルエーテル等のグリコールエーテル類、炭素数8までのアルコール類もしくはメチルアセテート、エチルアセテート、3−メトキシジブチルアセテート、2−エトキシメチルアセテート、2−エトキシエチルアセテート、プロピレンカーボネート等のエステル類、ジメチルホルムアミド等のアミド類が挙げられる。 The wet paint booth circulating water treatment agent of the present invention has a specific α-chlorobenzaldoxime compound, which is an active ingredient, which is hardly soluble in water. To form a dispersant prepared by dispersing in water. Hydrophilic solvents include alcohols such as methanol and ethanol, glycols such as ethylene glycol, propylene glycol, diethylene glycol and dipropylene glycol, methyl cellosolve, phenyl cellosolve, diethylene glycol monomethyl ether, dipropylene glycol monoethyl ether, and tripropylene glycol. Glycol ethers such as monomethyl ether, alcohols having up to 8 carbon atoms, methyl acetate, ethyl acetate, 3-methoxydibutyl acetate, 2-ethoxymethyl acetate, 2-ethoxyethyl acetate, esters such as propylene carbonate, dimethylformamide, etc. Of the amides.
分散剤の形態では、カチオン性界面活性剤、アニオン性界面活性剤、ノニオン性界面活性剤又は両性界面活性剤を用いて、有効成分である特定のα−クロロベンズアルドキシム化合物を水に分散させる。なかでも、ノニオン性界面活性剤が好ましく、高級アルコールのエチレンオキサイド付加物、アルキルフェノールのエチレンオキサイド付加物、脂肪酸のエチレンオキサイド付加物、多価アルコール脂肪酸エステルのエチレンオキサイド付加物、高級アルキルアミンのエチレンオキサイド付加物、脂肪酸アミドのエチレンオキサイド付加物、グリセリンの脂肪酸エステル、ペンタエリスリトールの脂肪酸エステル、ソルビトール及びソルビタンの脂肪酸エステル、ショ糖の脂肪酸エステル、多価アルコールのアルキルエーテル、アルキロールアミド等が挙げられる。 In the form of a dispersing agent, a specific α-chlorobenzaldoxime compound as an active ingredient is dispersed in water using a cationic surfactant, an anionic surfactant, a nonionic surfactant or an amphoteric surfactant. . Among these, nonionic surfactants are preferred, higher alcohol ethylene oxide adducts, alkylphenol ethylene oxide adducts, fatty acid ethylene oxide adducts, polyhydric alcohol fatty acid ester ethylene oxide adducts, higher alkylamine ethylene oxides. Examples include adducts, ethylene oxide adducts of fatty acid amides, fatty acid esters of glycerin, fatty acid esters of pentaerythritol, fatty acid esters of sorbitol and sorbitan, fatty acid esters of sucrose, alkyl ethers of polyhydric alcohols, alkylolamides, and the like.
湿式塗装ブースにおける本発明の湿式塗装ブース循環水処理剤の添加場所は特に限定されないが、処理剤がブース循環水中に混合され易い箇所であれば良く、循環ポンプの手前等が好ましい。また、添加方法についても特に限定はないが、定量ポンプで連続的に添加したり、間欠的に添加したりするなど適宜選択することができる。 Although the addition place of the wet coating booth circulating water treatment agent of this invention in a wet coating booth is not specifically limited, What is necessary is just a location with which a processing agent is easy to be mixed in booth circulating water, and the front of a circulation pump etc. are preferable. The addition method is not particularly limited, but can be appropriately selected such as continuous addition with a metering pump or intermittent addition.
本発明の湿式塗装ブース循環水処理剤の添加量は、処理対象の塗装ブースの形式、使用塗料、運転条件等によって異なるが、通常、ブース循環水に対して、特定のα−クロロベンズアルドキシム化合物の濃度として0.1〜100mg/Lであり、好ましくは1〜20mg/Lである。0.1mg/Lより少ない場合は十分な悪臭防止及び清澄化効果が得られない場合があり、また、100mg/Lより多い場合は、得られる効果は十分であるが、処理剤の添加量の増加に見合う効果の向上が得られない場合があり、経済的見地から好ましくない。 The amount of the wet coating booth circulating water treatment agent of the present invention varies depending on the type of coating booth to be treated, the paint used, the operating conditions, etc., but usually a specific α-chlorobenzaldoxime is added to the booth circulating water. The concentration of the compound is 0.1 to 100 mg / L, preferably 1 to 20 mg / L. When the amount is less than 0.1 mg / L, sufficient malodor prevention and clarification effects may not be obtained. When the amount is more than 100 mg / L, the obtained effect is sufficient. In some cases, the effect corresponding to the increase cannot be obtained, which is not preferable from an economic viewpoint.
本発明の湿式塗装ブース循環水処理剤には、本発明の効果を損なわない範囲で公知の他の成分を含むこともできる。公知の他の成分としては、製剤の安定性に寄与する粘度調整剤、消泡剤や殺菌剤などが挙げられる。 The wet coating booth circulating water treatment agent of the present invention may contain other known components as long as the effects of the present invention are not impaired. Examples of other known components include viscosity modifiers, antifoaming agents, and bactericides that contribute to the stability of the preparation.
本発明の湿式塗装ブース循環水処理方法は、特定のα−クロロベンズアルドキシム化合物を、湿式塗装ブース循環水に添加することを特徴とする湿式塗装ブース循環水処理方法であり、その添加方法は前記の特定のα−クロロベンズアルドキシム化合物を含有する塗装ブース循環水処理剤を用いても良いし、特定のα−クロロベンズアルドキシム化合物を、直接、湿式塗装ブース循環水に添加しても良いが、ブース循環水へのα−クロロベンズアルドキシム化合物の分散性を考慮すると、前記の塗装ブース循環水処理剤を使用することが好ましい。 The wet painting booth circulating water treatment method of the present invention is a wet painting booth circulating water treatment method characterized by adding a specific α-chlorobenzaldoxime compound to the wet painting booth circulating water, and the addition method is The coating booth circulating water treatment agent containing the specific α-chlorobenzaldoxime compound may be used, or the specific α-chlorobenzaldoxime compound may be added directly to the wet coating booth circulating water. Although it is good, considering the dispersibility of the α-chlorobenzaldoxime compound in the booth circulating water, it is preferable to use the coating booth circulating water treatment agent.
前記の塗装ブース循環水処理剤を使用する場合の添加箇所、添加方法及び添加濃度については前記のとおりであり、特定のα−クロロベンズアルドキシム化合物を、直接、湿式塗装ブース循環水に添加する場合も同様である。 The addition location, the addition method, and the addition concentration in the case of using the coating booth circulating water treatment agent are as described above, and the specific α-chlorobenzaldoxime compound is directly added to the wet coating booth circulating water. The same applies to the case.
本発明の湿式塗装ブース循環水処理方法においては、従来から湿式塗装ブースの処理剤として使用されている、塗料不粘着化剤、カチオン凝結剤、凝集剤等の公知の塗料処理剤や公知の消泡剤や殺菌剤等を併用できる。 In the wet paint booth circulating water treatment method of the present invention, known paint treating agents such as paint detackifying agents, cationic coagulants, and flocculants, which have been conventionally used as treatment agents for wet paint booths, and known dissipators. A foaming agent, a disinfectant, etc. can be used together.
塗料不粘着化剤としては、例えば、水酸化ナトリウム、ケイ酸ナトリウム、亜鉛酸ナトリウム、アルミナゾル、シリカゾル、アルミン酸ナトリウム、ポリ塩化アルミニウム、硫酸アルミニウム、塩化第二鉄、ポリ硫酸第二鉄、メラミン−ホルムアルデヒド縮合物、フェノール−ホルムアルデヒド縮合物、ベントナイト、セピオライト、高級アルコールもしくはその誘導体、高級脂肪酸もしくはその誘導体、ポリエチレンワックスもしくはその誘導体、パラフィンワックスもしくはその誘導体、ポリスチレンもしくはその誘導体、ポリビニルアルコールもしくはその誘導体、ジアリルジメチルアンモニウムクロライド−アクリルアミド共重合体等が挙げられる。中でも、アルミナゾル、アルミン酸ナトリウム、ポリ塩化アルミニウム、硫酸アルミニウム、メラミン−ホルムアルデヒド縮合物、フェノール−ホルムアルデヒド縮合物、高級脂肪酸もしくはその誘導体、ポリエチレンワックスもしくはその誘導体が、不粘着化効果ならびに清澄化効果を補う効果の上で好ましい。 Examples of the paint non-tackifier include sodium hydroxide, sodium silicate, sodium zincate, alumina sol, silica sol, sodium aluminate, polyaluminum chloride, aluminum sulfate, ferric chloride, polyferric sulfate, melamine- Formaldehyde condensate, phenol-formaldehyde condensate, bentonite, sepiolite, higher alcohol or derivative thereof, higher fatty acid or derivative thereof, polyethylene wax or derivative thereof, paraffin wax or derivative thereof, polystyrene or derivative thereof, polyvinyl alcohol or derivative thereof, diallyl Examples thereof include dimethylammonium chloride-acrylamide copolymer. Among them, alumina sol, sodium aluminate, polyaluminum chloride, aluminum sulfate, melamine-formaldehyde condensate, phenol-formaldehyde condensate, higher fatty acids or derivatives thereof, polyethylene wax or derivatives thereof supplement the non-adhesive effect and clarification effect. It is preferable in terms of effect.
カチオン凝結剤としては、例えば(メタ)アクリル酸エステル(炭素数1〜4のアルコールのエステル)・(メタ)アクリルアミノエチルトリメチルアンモニウム共重合体、(メタ)アクリルアミド・(メタ)アクリルアミノエチルトリメチルアンモニウム共重合体、(メタ)アクリルアミノジアルキル(炭素数1〜4のアルキル基)・(メタ)アクリルアミノエチルトリメチルアンモニウム共重合体、ポリ(メタ)アクリルアミノエチルトリメチルアンモニウム等の(メタ)アクリルアミノエチルトリメチルアンモニウム共重合体;ジシアンジアミド−ホルムアルデヒド縮合物、ジシアンジアミド−ジエチレントリアミン縮合物等のジシアンジアミド系縮合物;ジメチルアミン−エピクロロヒドリン縮合物、ジエチルアミン−エピクロロヒドリン縮合物、ジメチルアミン−エピクロルヒドリン−アンモニア縮合物、ジエチルアミン−エピクロルヒドリン−アンモニア縮合物等のジアルキルアミン−エピハロヒドリン縮合物;ポリジアリルジメチルアンモニウムクロライド、ジアリルジメチルアンモニウムクロライド−アクリルアミド共重合体、ジアリルジメチルアンモニウムクロライド−二酸化硫黄共重合体、ジアリルジメチルアンモニウムクロライド−(メタ)アクリルアミド共重合体、ジアリルジメチルアンモニウムクロライド−(メタ)アクリル酸共重合体、ジアリルジメチルアンモニウムクロライド−(メタ)アクリル酸−(メタ)アクリルアミド共重合体等のジアリルジメチルアンモニウムクロライド共重合体;ポリエチレンイミン、ポリアリルアミン、ポリビニルアミン等のポリアルキルアミンが挙げられる。 Examples of the cationic coagulant include (meth) acrylic acid ester (alcohol ester having 1 to 4 carbon atoms) / (meth) acrylaminoethyltrimethylammonium copolymer, (meth) acrylamide / (meth) acrylaminoethyltrimethylammonium Copolymer, (meth) acrylaminodialkyl (alkyl group having 1 to 4 carbon atoms) / (meth) acrylaminoethyltrimethylammonium copolymer, (meth) acrylaminoethyl such as poly (meth) acrylaminoethyltrimethylammonium Trimethylammonium copolymer; Dicyandiamide-based condensates such as dicyandiamide-formaldehyde condensate, dicyandiamide-diethylenetriamine condensate; dimethylamine-epichlorohydrin condensate, diethylamine-epichlorohi Dialkylamine-epihalohydrin condensates such as phosphorus condensate, dimethylamine-epichlorohydrin-ammonia condensate, diethylamine-epichlorohydrin-ammonia condensate; polydiallyldimethylammonium chloride, diallyldimethylammonium chloride-acrylamide copolymer, diallyldimethylammonium chloride- Sulfur dioxide copolymer, diallyldimethylammonium chloride- (meth) acrylamide copolymer, diallyldimethylammonium chloride- (meth) acrylic acid copolymer, diallyldimethylammonium chloride- (meth) acrylic acid- (meth) acrylamide copolymer Diallyldimethylammonium chloride copolymer such as a polymer; polyethyleneimine, polyallylamine, polyvinyl Polyalkyl amines such as emissions and the like.
これらの中でも、ポリアクリルアミノエチルトリメチルアンモニウムクロライド、ジシアンジアミド−ホルムアルデヒド縮合物、ジシアンジアミド−ジエチレントリアミン縮合物、ジメチルアミン−エピクロルヒドリン縮合物、ジメチルアミン−エピクロルヒドリン−アンモニア縮合物、ジアリルジメチルアンモニウムクロライド重合体、ジアリルジメチルアンモニウムクロライド−アクリルアミド共重合体、ジアリルジメチルアンモニウムクロライド−二酸化硫黄共重合体、ポリエチレンイミン、ポリビニルアミンは、カチオン強度が高いために好適である。 Among these, polyacrylaminoethyltrimethylammonium chloride, dicyandiamide-formaldehyde condensate, dicyandiamide-diethylenetriamine condensate, dimethylamine-epichlorohydrin condensate, dimethylamine-epichlorohydrin-ammonia condensate, diallyldimethylammonium chloride polymer, diallyldimethylammonium A chloride-acrylamide copolymer, diallyldimethylammonium chloride-sulfur dioxide copolymer, polyethyleneimine, and polyvinylamine are preferred because of their high cation strength.
カチオン凝結剤の分子量は、本発明に特に制限を加えるものでないが、2,000〜500,000の範囲が好ましい。分子量がこの範囲であれば、特に水性塗料の凝結効果に優れているからである。 The molecular weight of the cationic coagulant is not particularly limited, but is preferably in the range of 2,000 to 500,000. This is because if the molecular weight is within this range, the setting effect of the aqueous paint is particularly excellent.
凝集剤は、水溶性のアニオン系、カチオン系及び非イオン系高分子で、分子量が1,500,000〜20,000,000、好ましくは2,000,000〜15,000,000の水溶性高分子である。凝集剤は、塗料不粘着化剤及び/またはカチオン凝結剤によって、凝結・不粘着化させて固液分離した塗料粒子を架橋して粗大化し、回収をさらに容易にする効果を奏する。 The flocculant is a water-soluble anionic, cationic or nonionic polymer and has a molecular weight of 1,500,000 to 20,000,000, preferably 2,000,000 to 15,000,000. It is a polymer. The flocculant has an effect of further facilitating the recovery by cross-linking and coarsening the paint particles solidified and solidified by coagulation and non-adhesion with a paint non-tackifier and / or a cationic coagulant.
凝集剤としては、例えばポリアクリルアミド、アクリルアミド−アクリル酸共重合体、アクリルアミド−アクリルアミノエチルトリメチルアンモニウムクロライド共重合体、アクリルアミド−メタクリルアミノエチルトリメチルアンモニウムクロライド共重合体、アクリルアミド−[2−(アクリロイルオキシ)エチル]ベンジルジメチルアンモニウムクロライド・[2−(アクリロイルオキシ)エチル]トリメチルアンモニウム共重合体、アクリルアミド−ビニルスルフォン酸共重合体及びその塩、ポリビニルイミダゾリン、ポリエチレンオキシド等が挙げられる。 Examples of the flocculant include polyacrylamide, acrylamide-acrylic acid copolymer, acrylamide-acrylaminoethyltrimethylammonium chloride copolymer, acrylamide-methacrylaminoethyltrimethylammonium chloride copolymer, and acrylamide- [2- (acryloyloxy). And ethyl] benzyldimethylammonium chloride / [2- (acryloyloxy) ethyl] trimethylammonium copolymer, acrylamide-vinyl sulfonic acid copolymer and salts thereof, polyvinyl imidazoline, and polyethylene oxide.
これらの中でも、ポリアクリルアミド、アクリルアミド−アクリル酸共重合体、アクリルアミド−アクリルアミノエチルトリメチルアンモニウムクロライド共重合体、アクリルアミド−メタクリルアミノエチルトリメチルアンモニウムクロライド共重合体、アクリルアミド−[2−(アクリロイルオキシ)エチル]ベンジルジメチルアンモニウムクロライド・[2−(アクリロイルオキシ)エチル]トリメチルアンモニウム共重合体が好適である。 Among these, polyacrylamide, acrylamide-acrylic acid copolymer, acrylamide-acrylaminoethyltrimethylammonium chloride copolymer, acrylamide-methacrylaminoethyltrimethylammonium chloride copolymer, acrylamide- [2- (acryloyloxy) ethyl] A benzyldimethylammonium chloride / [2- (acryloyloxy) ethyl] trimethylammonium copolymer is preferred.
塗料不粘着化剤や凝集剤は、油性塗料単独使用、水性塗料単独使用及び水性塗料と油性塗料の混合使用のいずれの使用形態のブースにおいても使用でき、対象ブースの運転状況や設備状況に合わせて、適宜、薬剤の種類と組み合わせ、添加方法や添加量を選択できる。カチオン凝結剤は、主に水性塗料単独使用や水性塗料と油性塗料の混合使用の形態のブースにおいて使用され、カチオン凝結剤の添加量をブース循環水中の電荷量によって管理することも好ましい。ブース循環水中の電荷量はカチオン凝結剤の添加量によって大きく変化し、ブース循環水中の電荷量が−200〜+200μeq/Lとなるように添加すれば、塗料粒子が水中か分離しやすく、回収が極めて容易となる。 The paint detackifier and flocculant can be used in booths that use either oil paint alone, water paint alone, or mixed use of water paint and oil paint. Thus, the addition method and the addition amount can be selected as appropriate in combination with the kind of the drug. The cationic coagulant is mainly used in a booth in the form of a single use of an aqueous paint or a mixed use of an aqueous paint and an oil paint, and it is also preferable to control the addition amount of the cationic coagulant by the amount of charge in the booth circulating water. The amount of charge in the booth circulating water varies greatly depending on the amount of cationic coagulant added, and if the amount of charge in the booth circulating water is -200 to +200 μeq / L, the paint particles can be easily separated from the water and recovered. It becomes extremely easy.
カチオン凝結剤の添加量をブース循環水中の電荷量によって管理する場合、コロイド滴定法、粒子電荷測定法(PCD法)、電気泳動法等の方法で測定することができ、これらの方法は公知であるのでその詳細な記載は省略する。 When the amount of cationic coagulant added is controlled by the amount of charge in Booth circulating water, it can be measured by methods such as colloid titration, particle charge measurement (PCD method), electrophoresis, etc., and these methods are known. The detailed description thereof is omitted.
湿式塗装ブース循環水で使用する消泡剤や殺菌剤は、各種工業の工程水や排水等の水系で使用される一般的な公知の消泡剤や殺菌剤を適用できる。 As the antifoaming agent and disinfectant used in the wet paint booth circulating water, general known antifoaming agents and disinfecting agents used in water systems such as process water and waste water in various industries can be applied.
本発明の湿式塗装ブース循環水処理方法において、前記の塗料処理剤、消泡剤、殺菌剤等は、本発明の特定のα−クロロベンズアルドキシム化合物の適用に係わらず、従来からの適用方法を用いることができる。 In the wet coating booth circulating water treatment method of the present invention, the paint treatment agent, antifoaming agent, disinfectant and the like are applied in the conventional manner regardless of the application of the specific α-chlorobenzaldoxime compound of the present invention. Can be used.
以下に本発明を具体化した実施例を挙げて本発明を詳細に説明するが、本発明は以下の実施例に限定されるものではなく、また、特許請求の範囲の記載を逸脱せず、当業者が容易に想到できる範囲で種々の変形態様もこの発明に含まれる。 Hereinafter, the present invention will be described in detail by way of examples embodying the present invention. However, the present invention is not limited to the following examples, and does not depart from the description of the scope of claims. Various modifications as long as those skilled in the art can easily conceive are also included in the present invention.
(試験に用いる装置)
実施例及び比較例には、図1に示す試験用湿式塗装ブースを用いた。このブースは一般的な大型湿式塗装ブースを模しており、塗装室1と循環水ピット2と濃縮回収槽3を備える。塗装室1では塗料4が噴霧され、未塗着塗料は接触部5にて塗装室1に供給されたブース循環水6と接触して捕集され、循環水ピット2に流下する。尚、この試験用湿式塗装ブースでは、被塗装物は無く、噴霧された塗料は、全量、未塗着塗料となる。接触部5にてブース循環水6に捕集された未塗着塗料は循環水ピット2でスラッジ状に浮上分離し、ブース循環水と共に濃縮回収槽送りポンプ7で吸引されて濃縮回収槽3に送られる。濃縮回収槽3では加圧浮上作用により未塗着塗料のスラッジが濃縮され、濃縮スラッジ8は回収されて系外に搬出される。一方、濃縮回収槽3においてスラッジと分離した処理水9は循環水ピット2に戻る。循環水ピット2に貯留されたブース循環水は、循環ポンプ10によってブース循環水6として塗装室に送出される。11、12、13は実施例及び比較例における薬剤の添加箇所であり、添加箇所11では本発明の処理剤やカチオン凝結剤が添加され、添加箇所12では塗料不粘着化剤が添加され、添加箇所13では凝集剤が添加される。この試験用湿式塗装ブースの保有水量は500Lであり、循環ポンプ10によるブース循環水の循環水量は100L/分、濃縮回収槽送りポンプ7による濃縮回収槽3への送水量は30L/分の運転条件で、全ての実施例、比較例の試験を行った。(Equipment used for testing)
In the examples and comparative examples, the test wet coating booth shown in FIG. 1 was used. This booth simulates a general large-scale wet painting booth, and includes a
(実施例及び比較例に使用した薬剤)
(A)本発明の処理剤及び従来公知の悪臭防止剤
A−1:α−クロロ−p−クロロベンズアルドキシム2重量部をジエチレングリコール
98重量部に溶解して調製した薬剤(本発明の処理剤)
A−2:α−クロロベンズアルドキシム2重量部をジエチレングリコール98重量部に
溶解して調製した薬剤(本発明の処理剤)
A−3:α−クロロベンズアルドキシムアセテート2重量部をジエチレングリコール
98重量部に溶解して調製した薬剤(本発明の処理剤)
A−4:ヘキサヒドロ−1,3,5−トリス(2−ヒドロキシエチル)−S−トリアジン
2重量部と水酸化ナトリウム5重量部を純水93重量部に溶解して調製した薬剤
(従来公知の悪臭防止剤)
A−5:トリ−n−ブチル−n−ヘキサデシルホスホニウムクロライド2重量部を純水
98重量部に溶解して調製した薬剤(従来公知の悪臭防止剤)
(B)塗料不粘着化剤
B−1:メラミン−ホルムアルデヒド縮合物〔伯東(株)製「ハクトロンS−830」〕
B−2:ポリ塩化アルミニウム液(有効成分:Al2O3として10〜11%含有)
B−3:硫酸アルミニウム液(有効成分:Al2O3として8%含有)
B−4:アルミナゾル〔伯東(株)製「ハクトロンS−600」〕
B−5:ポリエチレンワックス乳化物〔明成化学工業(株)製「メイカテックスPEC−
270」〕
(C)カチオン凝結剤
C−1:ジメチルアミン−エピクロルヒドリン縮合物〔長瀬産業(株)製「ワイステック
スT−101−50」〕
C−2:ポリエチレンイミン〔日本触媒(株)製「エポミンP−1000」〕
C−3:ジアリルジメチルアンモニウムクロライド−アクリルアミド共重合体〔センカ
(株)製「センカフロックDC−7513」〕
(D)凝集剤
D−1:アクリルアミド−アクリルアミノエチルトリメチルアンモニウムクロライド共重
合体〔MTアクアポリマー(株)製「アロンフロック3390」〕
D−2:アクリルアミド−アクリル酸共重合体〔MTアクアポリマー(株)製「アコフロ
ック2360」〕(Drugs used in Examples and Comparative Examples)
(A) Treatment agent of the present invention and conventionally known malodor control agent A-1: Agent prepared by dissolving 2 parts by weight of α-chloro-p-chlorobenzaldoxime in 98 parts by weight of diethylene glycol (treatment agent of the present invention )
A-2: Agent prepared by dissolving 2 parts by weight of α-chlorobenzaldoxime in 98 parts by weight of diethylene glycol (the treatment agent of the present invention)
A-3: Agent prepared by dissolving 2 parts by weight of α-chlorobenzaldoxime acetate in 98 parts by weight of diethylene glycol (treatment agent of the present invention)
A-4: Drug prepared by dissolving 2 parts by weight of hexahydro-1,3,5-tris (2-hydroxyethyl) -S-triazine and 5 parts by weight of sodium hydroxide in 93 parts by weight of pure water (known in the art) Odor control agent)
A-5: Drug prepared by dissolving 2 parts by weight of tri-n-butyl-n-hexadecylphosphonium chloride in 98 parts by weight of pure water (previously known malodor control agent)
(B) Paint detackifying agent B-1: Melamine-formaldehyde condensate [“Haktron S-830” manufactured by Hakuto Co., Ltd.]
B-2: poly aluminum chloride solution (active ingredient: 10 to 11% containing as Al 2 O 3)
B-3: Aluminum sulfate solution (active ingredient: contained 8% as Al 2 O 3 )
B-4: Alumina sol [“Hakutron S-600” manufactured by Hakuto Co., Ltd.]
B-5: Polyethylene wax emulsion [Maisei Chemical Co., Ltd. "Meikatex PEC-
270 ")
(C) Cationic coagulant C-1: Dimethylamine-epichlorohydrin condensate [“Wastex T-101-50” manufactured by Nagase & Co., Ltd.]
C-2: Polyethyleneimine [“Epomin P-1000” manufactured by Nippon Shokubai Co., Ltd.]
C-3: diallyldimethylammonium chloride-acrylamide copolymer [Senka Co., Ltd. “Senka Flock DC-7513”]
(D) Flocculant D-1: Acrylamide-acrylaminoethyltrimethylammonium chloride copolymer [“Aron Flock 3390” manufactured by MT Aquapolymer Co., Ltd.]
D-2: Acrylamide-acrylic acid copolymer ["Acofloc 2360" manufactured by MT Aquapolymer Co., Ltd.]
1.実機ブース循環水の悪臭防止及び清澄化試験
(実施例1)
某自動車工場の、水性塗料と油性塗料の混合使用湿式塗装ブースの循環水を使用した。この塗装ブースでは、水性塗料の自動車用水性上塗り塗料(日本ペイント(株)製)と、油性塗料の自動車用溶剤クリア塗料(関西ペイント(株)製)を使用しており、そのブース循環水は半年間入れ替えを行っておらず、強烈な悪臭と高濃度の濁質を有していた。このブース循環水500Lを図1に示す試験用湿式塗装ブースの循環水ピット2に投入し、循環ポンプ10によって100L/分でブース循環水を循環させ、また、濃縮回収槽送りポンプ7によって濃縮回収槽3へ30L/分で送水し、濃縮回収槽3で加圧浮上作用により循環水中の濁質を濃縮し、濃縮スラッジ8を回収して系外に搬出する。この系に、本発明の処理剤として、A−1を、1日に1回、ブース循環水に対して、有効成分として10mg/Lになるように、添加箇所11から添加した。本試験では塗料は噴霧せず、また、本発明の処理剤以外の薬剤も添加しなかった。試験中の揮発や飛散及びスラッジに同伴して系外に除去される水分については、循環水ピット2の水位を維持するように清水を補充した。試験用湿式塗装ブースを3日間継続運転した後、ブース循環水を採取し、濁度を測定するとともに、臭気の官能評価を行い、6段階臭気強度表示法にて臭気強度を判定した。1. Odor control and clarification test of actual machine booth circulating water (Example 1)
循環 Used circulating water from a wet painting booth using a mixture of water-based paint and oil-based paint at an automobile factory. This paint booth uses water-based water-based topcoat paint for automobiles (manufactured by Nippon Paint Co., Ltd.) and oil-based paint solvent clear paint for automobiles (manufactured by Kansai Paint Co., Ltd.). It was not replaced for half a year and had a strong odor and a high concentration of turbidity. 500 L of this booth circulating water is put into the circulating
(比較例1)
比較例1では、添加する薬剤を、A−1に代えて、A−4を、1日に1回、有効成分としてブース循環水に対して10mg/Lになるように、添加箇所11から添加した以外は、実施例1と同様に試験を行った。(Comparative Example 1)
In Comparative Example 1, the drug to be added is replaced with A-1, and A-4 is added once a day as an active ingredient from the addition site 11 so as to be 10 mg / L with respect to the booth circulating water. The test was performed in the same manner as in Example 1 except that.
(比較例2)
比較例2では、添加する薬剤を、A−1に代えて、A−5を、1日に1回、有効成分としてブース循環水に対して10mg/Lになるように、添加箇所11から添加した以外は、実施例1と同様に試験を行った。(Comparative Example 2)
In Comparative Example 2, the drug to be added was replaced with A-1, and A-5 was added from the addition site 11 once a day so that the active ingredient was 10 mg / L with respect to the booth circulating water. The test was performed in the same manner as in Example 1 except that.
(比較例3)
比較例3では、本発明の処理剤を添加せず、また、他の薬剤も添加せず、実施例1と同様に試験を行った。即ち、無処理の例である。(Comparative Example 3)
In Comparative Example 3, the test was performed in the same manner as in Example 1 without adding the treatment agent of the present invention and without adding other chemicals. In other words, this is an example of no processing.
実施例1、比較例1〜3の試験終了後のブース循環水の濁度測定結果と臭気強度の判定結果を表1に示した。 Table 1 shows the turbidity measurement results and the odor intensity determination results of the booth circulating water after completion of the tests of Example 1 and Comparative Examples 1 to 3.
表1の結果より、本発明の、特定のα−クロロベンズアルドキシム化合物を含有する湿式塗装ブース循環水処理剤は、従来公知の悪臭防止剤に比べて、悪臭防止効果も優れているが、特に従来公知の悪臭防止剤では得られない、顕著なブース循環水の清澄化効果を示すことが明らかになった。 From the results shown in Table 1, the wet paint booth circulating water treatment agent containing the specific α-chlorobenzaldoxime compound of the present invention has an excellent malodor prevention effect as compared with a conventionally known malodor prevention agent. In particular, it has been revealed that a remarkable booth circulating water clarification effect that cannot be obtained with a conventionally known malodor control agent is exhibited.
2.ブース循環水の処理試験(1)(水性塗料、油性塗料混合条件)
(実施例2)
図1に示す試験用湿式塗装ブースの循環水ピット2に清水500Lを投入し、循環ポンプ10によって100L/分でブース循環水を循環させ、また、濃縮回収槽送りポンプ7によって濃縮回収槽3へ30L/分で送水し、濃縮回収槽3で加圧浮上作用により循環水中の濁質を濃縮し、濃縮スラッジ8を回収して系外に搬出する。この系に、表3の実施例2に示す添加薬剤を表3の実施例2に示す添加量で添加しながら、塗装室1内で、ブース循環水に向けて水性塗料と油性塗料とを各5g/分で連続して1日5時間噴霧した。水性塗料としては、自動車用水性上塗り塗料(日本ペイント(株)製)を用い、油性塗料としては、自動車用溶剤クリア塗料(日本ペイント(株)製)を用いた。ここで、本発明の処理剤である、添加薬剤A−1は、1日に1回、ブース循環水に対して、有効成分として10mg/Lになるように、添加箇所11から添加した。また、添加薬剤B−1は、塗装ブースで噴霧された総塗料(=水性塗料+油性塗料)重量に対して、有効成分として1重量%を、噴霧の間、添加箇所12から添加した。添加薬剤C−1は、塗装ブースで噴霧された水性塗料重量に対して、有効成分として1重量%を、噴霧の間、添加箇所11から添加した。添加薬剤D−1は、塗装ブースで噴霧された総塗料(=水性塗料+油性塗料)重量に対して、有効成分として0.3重量%を、噴霧の間、添加箇所13から添加した。尚、塗料を噴霧している間、ブース循環水の電荷を測定し、電荷が−200〜+200(μeq/L−ブース循環水)になるようにカチオン凝結剤を添加したが、この添加量は、予備試験によって、ブース循環水の電荷が所定の電荷範囲に入るカチオン凝結剤の添加量を予め確認し、表3に示すカチオン凝結剤の添加量を決めている。ブース循環水の電荷はコロイド滴定により測定した。試験中の揮発や飛散及びスラッジに同伴して系外に除去される水分については、循環水ピット2の水位を維持するように清水を補充した。試験用湿式塗装ブースを14日間継続運転した後、ブース循環水を採取し、濁度を測定するとともに、臭気の官能評価を行い、6段階臭気強度表示法にて臭気強度を判定した。2. Booth circulating water treatment test (1) (water paint and oil paint mixing conditions)
(Example 2)
500 L of fresh water is introduced into the circulating
(実施例3〜13、比較例4〜6)
実施例3〜13、比較例4〜6では、表3の各実施例及び各比較例に示す添加薬剤を表3の各実施例及び各比較例に示す添加量で添加した以外は、実施例2と同様にブース循環水の処理試験(1)を行って、試験結果を得た。(Examples 3 to 13, Comparative Examples 4 to 6)
In Examples 3 to 13 and Comparative Examples 4 to 6, Examples were added except that the additive agents shown in each Example and each Comparative Example in Table 3 were added in the addition amounts shown in each Example and each Comparative Example in Table 3. The treatment test (1) of the booth circulating water was conducted in the same manner as 2 and the test results were obtained.
(比較例7)
比較例7では、薬剤を添加せずに、ブース循環水の処理試験(1)を行って、試験結果を得た。即ち、無処理の例である。(Comparative Example 7)
In Comparative Example 7, the treatment test (1) of the booth circulating water was performed without adding the chemical, and the test result was obtained. In other words, this is an example of no processing.
実施例2〜13、比較例4〜7の試験終了後のブース循環水の濁度測定結果と臭気強度の判定結果、及び試験中のブース循環水の電荷の平均値を表3に示した。 Table 3 shows the turbidity measurement results and the odor intensity determination results of the booth circulating water after the tests of Examples 2 to 13 and Comparative Examples 4 to 7, and the average value of the charge of the booth circulating water during the test.
(2)臭気強度の官能評価は表2に従った。
(2) Sensory evaluation of odor intensity was in accordance with Table 2.
表3に示すように、本発明の処理剤と、塗料不粘着化剤及び/またはカチオン凝結剤及び/または凝集剤を添加して、ブース循環水の電荷が−200〜+200(μeq/L−ブース循環水)になるようにカチオン凝結剤の添加量を調節した実施例2〜13では、濁度が110度以下、臭気強度が2以下の優れた効果を示した。
一方、比較例4は、本発明の処理剤を添加せず、塗料不粘着化剤、カチオン凝結剤及び凝集剤を添加して、ブース循環水の電荷を適正範囲に調節したものであるが、濁度が285度と高いうえ、臭気強度も3〜4と高く、ブース循環水の清澄性が十分でなく、臭いことが判る。また、比較例5あるいは比較例6は、従来公知の悪臭防止剤と、塗料不粘着化剤、カチオン凝結剤及び凝集剤を添加して、ブース循環水の電荷を適正範囲に調節したものであるが、濁度が282〜310度と高いうえ、臭気強度も3〜4と高く、ブース循環水の清澄性が十分でなく、臭いことが判る。
以上の実施例2〜13と比較例4〜7の結果比較から、本発明の、湿式塗装ブース循環水に対する優れた清澄化効果及び悪臭防止効果が明確に示された。As shown in Table 3, the charge of the booth circulating water is −200 to +200 (μeq / L− by adding the treatment agent of the present invention and / or the paint tackifier and / or the cationic coagulant and / or the flocculant. In Examples 2 to 13 in which the addition amount of the cationic coagulant was adjusted so as to be a booth circulating water), excellent effects were exhibited with a turbidity of 110 degrees or less and an odor intensity of 2 or less.
On the other hand, in Comparative Example 4, the treatment agent of the present invention was not added, and the paint detackifying agent, the cationic coagulant and the flocculant were added to adjust the booth circulating water charge to an appropriate range. The turbidity is as high as 285 degrees, and the odor intensity is as high as 3 to 4, so that the clarity of the booth circulating water is not sufficient, and it can be seen that it is odorous. In Comparative Example 5 or Comparative Example 6, the charge of Booth circulating water is adjusted to an appropriate range by adding a conventionally known malodor prevention agent, a coating tackifier, a cationic coagulant and a flocculant. However, the turbidity is as high as 282 to 310 degrees, the odor intensity is as high as 3 to 4, and the clearness of the booth circulating water is not sufficient, and it can be seen that it is odorous.
From the result comparison of the above Examples 2-13 and Comparative Examples 4-7, the outstanding clarification effect with respect to the wet coating booth circulating water and the malodor prevention effect of this invention were shown clearly.
3.ブース循環水の処理試験(2)(油性塗料単独条件)
(実施例14〜18、比較例8〜10)
実施例14〜18、比較例8〜10では、噴霧する塗料とその噴霧量を「水性塗料と油性塗料とを各5g/分」から「油性塗料を10g/分」に変更し、かつ、表4の各実施例及び各比較例に示す添加薬剤を表4の各実施例及び各比較例に示す添加量で添加した以外は、実施例2と同様に試験を行って、ブース循環水の処理試験(2)の試験結果を得た。表4に示すカチオン凝結剤の添加量を決め方も実施例2に準じた。油性塗料としては、自動車用溶剤中塗り塗料(関西ペイント(株)製)を用いた。3. Booth circulating water treatment test (2) (oil paint alone condition)
(Examples 14-18, Comparative Examples 8-10)
In Examples 14 to 18 and Comparative Examples 8 to 10, the paint to be sprayed and the spray amount thereof were changed from “5 g / min each for water-based paint and oil-based paint” to “10 g / min for oil-based paint”, and The test was performed in the same manner as in Example 2 except that the additive agents shown in each Example 4 and each Comparative Example were added in the addition amounts shown in each Example and each Comparative Example in Table 4, and the booth circulating water was treated. The test result of test (2) was obtained. The method of determining the addition amount of the cationic coagulant shown in Table 4 was also in accordance with Example 2. As the oil-based paint, an automotive solvent intermediate coating (manufactured by Kansai Paint Co., Ltd.) was used.
(比較例11)
比較例11では、薬剤を添加せずに、ブース循環水の処理試験(2)を行って、試験結果を得た。即ち、無処理の例である。(Comparative Example 11)
In Comparative Example 11, the treatment test (2) of the booth circulating water was performed without adding the chemical, and the test result was obtained. In other words, this is an example of no processing.
実施例14〜18、比較例8〜11の試験終了後のブース循環水の濁度測定結果と臭気強度の判定結果、及び試験中のブース循環水の電荷の平均値を表4に示した。 Table 4 shows the turbidity measurement results and the odor intensity determination results of the booth circulating water after the tests of Examples 14 to 18 and Comparative Examples 8 to 11, and the average value of the charge of the booth circulating water during the test.
(2)臭気強度の官能評価は表2に従った。
(2) Sensory evaluation of odor intensity was in accordance with Table 2.
表4に示すように、本発明の実施例14〜18では、濁度が60度以下、臭気強度が2以下の優れた効果を示した。一方、本発明の処理剤を添加しない比較例8〜10では、濁度が180度以上、臭気強度が3であり、ブース循環水の清澄性が十分でなく、臭いことが判る。以上の実施例14〜18と比較例8〜11の結果比較から、本発明の、湿式塗装ブース循環水に対する優れた清澄化効果及び悪臭防止効果が明確に示された。 As shown in Table 4, in Examples 14 to 18 of the present invention, excellent effects with turbidity of 60 degrees or less and odor intensity of 2 or less were exhibited. On the other hand, in Comparative Examples 8 to 10 in which the treatment agent of the present invention is not added, the turbidity is 180 degrees or more, the odor intensity is 3, the clarity of the booth circulating water is not sufficient, and it can be seen that the odor is present. From the result comparison of the above Examples 14-18 and Comparative Examples 8-11, the outstanding clarification effect and malodor prevention effect with respect to the wet painting booth circulating water of this invention were shown clearly.
4.ブース循環水の処理試験(3)(水性塗料単独条件)
(実施例19〜22、比較例12〜14)
実施例19〜22、比較例12〜14では、噴霧する塗料とその噴霧量を「水性塗料と油性塗料とを各5g/分」から「水性塗料を10g/分」に変更し、かつ、表5の各実施例及び各比較例に示す添加薬剤を表5の各実施例及び各比較例に示す添加量で添加した以外は、実施例2と同様に試験を行って、ブース循環水の処理試験(3)の試験結果を得た。表5に示すカチオン凝結剤の添加量を決め方も実施例2に準じた。水性塗料としては、自動車用水性上塗り塗料(関西ペイント(株)製)を用いた。4). Booth circulating water treatment test (3) (water-based paint single condition)
(Examples 19-22, Comparative Examples 12-14)
In Examples 19 to 22 and Comparative Examples 12 to 14, the paint to be sprayed and the spray amount thereof were changed from “5 g / min each for water-based paint and oil-based paint” to “10 g / min for water-based paint”, and The test was performed in the same manner as in Example 2 except that the additive chemicals shown in each Example 5 and each Comparative Example were added in the addition amounts shown in each Example and each Comparative Example in Table 5, and the booth circulating water was treated. The test result of test (3) was obtained. The method for determining the addition amount of the cationic coagulant shown in Table 5 was also in accordance with Example 2. As the water-based paint, a water-based top coat for automobiles (manufactured by Kansai Paint Co., Ltd.) was used.
(比較例15)
比較例15では、薬剤を添加せずに、ブース循環水の処理試験(3)を行って、試験結果を得た。即ち、無処理の例である。(Comparative Example 15)
In Comparative Example 15, the booth circulating water treatment test (3) was performed without adding any chemicals, and the test results were obtained. In other words, this is an example of no processing.
実施例19〜22、比較例12〜15の試験終了後のブース循環水の濁度測定結果と臭気強度の判定結果、及び試験中のブース循環水の電荷の平均値を表5に示した。 Table 5 shows the turbidity measurement results and the odor intensity determination results of the booth circulating water after the tests of Examples 19 to 22 and Comparative Examples 12 to 15, and the average value of the charge of the booth circulating water during the test.
(2)臭気強度の官能評価は表2に従った。
(2) Sensory evaluation of odor intensity was in accordance with Table 2.
表5に示すように、本発明の実施例19〜22では、濁度が40度以下、臭気強度が1以下の優れた効果を示した。一方、本発明の処理剤を添加しない比較例12〜14では、濁度が230度以上、臭気強度が3〜4であり、ブース循環水の清澄性が十分でなく、臭いことが判る。以上の実施例19〜22と比較例12〜15の結果比較から、本発明の、湿式塗装ブース循環水に対する優れた清澄化効果及び悪臭防止効果が明確に示された。 As shown in Table 5, in Examples 19 to 22 of the present invention, excellent effects with turbidity of 40 degrees or less and odor intensity of 1 or less were shown. On the other hand, in Comparative Examples 12 to 14 in which the treatment agent of the present invention is not added, the turbidity is 230 degrees or more, the odor intensity is 3 to 4, the clarity of the booth circulating water is not sufficient, and it can be seen that it is odorous. From the result comparison of the above Examples 19-22 and Comparative Examples 12-15, the outstanding clarification effect and the malodor prevention effect with respect to the wet coating booth circulating water of this invention were shown clearly.
本発明は、特に水性塗料の使用によりブース循環水の悪臭や濁質問題が深刻化している湿式塗装ブースに適用して、優れた悪臭防止効果と清澄化効果を得ることができる。 The present invention can be applied to a wet painting booth where the bad smell and turbidity problem of the circulating water of the booth is particularly serious due to the use of the water-based paint, and can obtain an excellent bad smell prevention effect and clarification effect.
1.塗装室
2.循環水ピット
3.濃縮回収槽
4.塗料
5.接触部
6.ブース循環水
7.濃縮回収槽送りポンプ
8.濃縮スラッジ
9.処理水
10.循環ポンプ
11.12.13.薬剤添加箇所1. Painting room Circulating
Claims (4)
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KR (2) | KR20160106168A (en) |
CN (1) | CN106458639A (en) |
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CN108778444A (en) * | 2016-03-31 | 2018-11-09 | 栗田工业株式会社 | The processing method of wet coating chamber circulating water inorganic agent and wet coating chamber circulating water |
JP6389978B1 (en) * | 2018-07-10 | 2018-09-12 | 伯東株式会社 | Wet paint booth circulating water treatment agent and treatment method |
JP7229055B2 (en) * | 2019-03-22 | 2023-02-27 | 伯東株式会社 | Wet paint booth circulating water treatment agent and treatment method |
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JPS6174607A (en) | 1984-09-19 | 1986-04-16 | Hakutou Kagaku Kk | Treatment of circulating water in wet painting booth |
JPS6342706A (en) | 1986-08-06 | 1988-02-23 | Kurita Water Ind Ltd | Treatment of water containing water-based paint |
JP3086062B2 (en) * | 1992-05-28 | 2000-09-11 | 株式会社片山化学工業研究所 | Antifouling agent for marine fouling organisms |
JP3177862B2 (en) * | 1992-06-30 | 2001-06-18 | 株式会社パーマケム・アジア | Slime control agent for papermaking |
JPH0631281A (en) | 1992-07-22 | 1994-02-08 | Sanai Sekiyu Kk | Additive for circulating water of wet coating booth |
US5397804A (en) * | 1993-03-19 | 1995-03-14 | Katayama Chemical Incorporated | Industrial microbicide and a method for killing microbes for industrial use |
JP2891635B2 (en) * | 1994-06-28 | 1999-05-17 | ソマール株式会社 | Industrial fungicides |
JP2940795B2 (en) * | 1994-06-28 | 1999-08-25 | ソマール株式会社 | Industrial fungicides |
JPH08323255A (en) | 1995-05-31 | 1996-12-10 | Otsuka Hake Seizo Kk | Apparatus for purifying coating booth |
JP3719276B2 (en) * | 1995-10-12 | 2005-11-24 | 株式会社パーマケム・アジア | Slime control agent for papermaking |
JPH10109907A (en) * | 1996-10-04 | 1998-04-28 | Katayama Chem Works Co Ltd | Microvicidal and bacteriostatic agent for industrial purpose and process therefor |
JPH11269012A (en) * | 1998-03-24 | 1999-10-05 | Somar Corp | Exterminating agent for noxious microoorganism |
JP2003267941A (en) * | 2002-03-14 | 2003-09-25 | Katayama Chem Works Co Ltd | METHOD FOR INDUSTRIALLY PRODUCING alpha-CHLOROBENZALDOXIME |
JP3531645B1 (en) * | 2003-01-16 | 2004-05-31 | ユケン工業株式会社 | Painting booth water treatment agent and treatment method |
JP2007238537A (en) * | 2006-03-10 | 2007-09-20 | K I Chemical Industry Co Ltd | Additive for circulating water in coating booth, method for treating water and circulating water for coating booth |
JP4697131B2 (en) * | 2006-12-15 | 2011-06-08 | 栗田工業株式会社 | Wet paint booth circulating water treatment agent and wet paint booth circulating water treatment method |
CN101830548A (en) * | 2010-05-25 | 2010-09-15 | 武汉理工大学 | Paint mist coagulant |
JP5990706B2 (en) * | 2011-11-30 | 2016-09-14 | 株式会社片山化学工業研究所 | Method for suppressing hydrogen sulfide generation in sludge treatment process |
CN102603108B (en) * | 2012-03-27 | 2014-05-21 | 郑州爱沃特环保科技有限公司 | Circulating water treatment system of wet-type spray booth and treatment method |
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CN106458639A (en) | 2017-02-22 |
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