JPH0553828B2 - - Google Patents

Info

Publication number
JPH0553828B2
JPH0553828B2 JP4237584A JP4237584A JPH0553828B2 JP H0553828 B2 JPH0553828 B2 JP H0553828B2 JP 4237584 A JP4237584 A JP 4237584A JP 4237584 A JP4237584 A JP 4237584A JP H0553828 B2 JPH0553828 B2 JP H0553828B2
Authority
JP
Japan
Prior art keywords
acid
treatment method
waste
strong
stirring
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP4237584A
Other languages
Japanese (ja)
Other versions
JPS60186546A (en
Inventor
Akira Iwata
Shuhei Tanimori
Tsutomu Kobayashi
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.)
LION ENG KK
Original Assignee
LION ENG KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by LION ENG KK filed Critical LION ENG KK
Priority to JP59042375A priority Critical patent/JPS60186546A/en
Publication of JPS60186546A publication Critical patent/JPS60186546A/en
Publication of JPH0553828B2 publication Critical patent/JPH0553828B2/ja
Granted legal-status Critical Current

Links

Classifications

    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は工場の塗装工程において発生する塗料
滓の処理方法に関するものである。自動車・電気
機器・建材等量産工場の塗装工程では多く熱硬化
型樹脂塗料の噴霧塗装が行なわれるが、この際に
塗料滓が発生する。例えば塗料滓が多量に発生す
る自動車車体の噴霧塗装では、塗装ブースにおい
てオーバースプレーで車体に付着せずに空中に浮
遊している塗料(上塗り用の焼付塗料が多い)の
ミストは水膜により捕集され分離ピツトに送ら
れ、ピツト内で一部は浮遊し、一部は沈殿して水
分30〜50%の粘着性の強い泥状まではガム状の塗
料滓となる。 従来からこのように捕収された塗料滓を有効に
利用するための種々の提案はあるが(例えば特公
昭52−35373)高い粘性と強い付着性のため取扱
いがむずかしく、実際には有効利用されないまま
焼却あるいは埋立により処理されているのが実状
である。しかし滓の性状が上記のようなものであ
るため焼却あるいは埋立に際しての取扱いは多く
の労力を要しており、殊に焼却する場合には熱に
より軟化流動して異常燃焼を起したり、また分解
して有害ガスを発生するなど燃焼管理が極めてむ
づかしく、特殊な燃焼炉を必要とする。 本発明はこのような塗料滓を粘着性がなく、加
熱により軟化流動することのないスポンジ状の粒
子とする塗料滓の処理方法を提供するもので、そ
の目的は塗料滓を取扱い易い形態とすることによ
り有効な資源として回収活用を円滑かつ経済的に
実施するにある。そして本発明にいうスポンジ状
の粒子とは、構造がスポンジ状というのではな
く、触感がスポンジ状である粒子の意であつて、
粒子も個々には不整形であり、粒度も必ずしも一
定せず、又小粒子の凝集体の粒子をも包含してお
り、色も特定されていないものを意味する。 塗料滓を有効活用するには、その取扱作業を容
易にする必要があり、まず粘着性を減少させるこ
とを実験検討した結果、アルカリ又は酸を添加し
て加熱すると容易に粘着性が消失することが判明
した。粘着性の消失はアルカリ又は酸により塗料
滓の樹脂成分が変化して硬化が促進されことによ
ると考えられるが、反応機構に関しては詳かでは
ない。アルカリを加えて加熱撹拌した場合は塗料
滓の如何により差はあるが一般的にはペースト状
となり硬化は顕著には進行しないが、しかし酸の
場合には共存する水を包含したスポンジ状に変化
し、撹拌の状況により粒径は変るが、それぞれ粒
径のほぼそろつた粒子となる。この粒子は塗料滓
のもつ粘着性・熱軟化性が全くないので、搬送・
貯蔵が容易であり、乾燥・粉砕して充填剤として
利用したり、或いは燃焼処理する場合においても
何ら支障なく処理することができる。したがつて
塗料滓の回収、ひいてはその活用を円滑かつ経済
的に行うことが可能となる。 強酸としては鉱酸あるいは有機酸の何れも使用
できるが、塩酸、硫酸、パラトルエンスルホン酸
などの強酸が適して居り、入手の容易さ、取り扱
い易さ、価格の面から硫酸が最も適している。こ
の酸は一般に市販されている濃度のもの、或は場
合によつては強酸性を維持する廃酸をそのまま、
あるいは水で稀釈して使用する。酸を稀釈して添
加した方が水分が多くなり流動性がよいので工程
全般を通じて撹拌が容易である。 この酸の添加量は塗料滓に対して1%以上添加
するが、塗料滓のもつ30〜50%の水分により稀釈
されるので、酸を稀釈して添加する場合は最終の
酸濃度が3%以上になるよう調整することが望ま
しい。 温度は50℃以下では硬化が遅く、90℃以上では
樹脂成分が分解してホルムアルデヒド、アクロレ
インなどの有害ガスの発生が激しくなるので、加
熱撹拌は50〜80℃が好ましい。硬化反応が進行す
ると水を内包したスポンジ状の粒子となり粘着性
が消失する。粒子の大きさは撹拌の強さにより変
化し、大きなせん断力を与えるような撹拌あるい
は磨砕するような混合撹拌を行なうと微細な粒子
となる。 この硬化反応の際に少量の界面活性剤を添加し
て加熱撹拌し僅かに発泡させると、反応物の流動
性が増し撹拌混合状態はより良好となる。界面活
性剤は陰イオン型・陽イオン型・非イオン型など
何れでも良いが、例えばドデシルトリメチルアン
モニウムクロリドを塗料滓に対して0.05〜1%添
加する。著しく発泡するような撹拌或いは界面活
性剤の過剰な添加は反応物が槽から溢出するので
作業上好ましくない。 酸処理した塗料滓に残存する酸は水酸化ナトリ
ウムなどのアルカリで中和してもよいし、あるい
は水洗により除去することもできる。 以上の如き本発明の処理で得られた粗粒は非粘
着性の粒子であるから、その粒子のままでの廃棄
処理が極めて容易であり、又それ自体かなりのカ
ロリーと有価無機物を含むので、焼却により有価
物の回収及び熱源としての利用も可能である。従
つて本発明の効果は極めて大きい。 実施例 1 塗料滓(顔料12%、熱硬化性樹脂48%、溶剤9
%、水31%)50gに表1に示す酸5g、水25gを
加えて、70〜80℃に加熱撹拌した。結果を表1に
示す。
The present invention relates to a method for treating paint slag generated in a factory painting process. In the painting process of mass-producing factories for automobiles, electrical equipment, building materials, etc., thermosetting resin paint is often sprayed, and paint slag is generated during this process. For example, in spray painting of automobile bodies, where a large amount of paint scum is generated, the mist of paint (often baked paint for topcoat) that does not adhere to the car body due to overspray and is suspended in the air in the paint booth is captured by a water film. The paint slag is collected and sent to a separation pit, where some of it floats and some of it settles down to a sticky mud with a moisture content of 30 to 50%. Although there have been various proposals for effectively utilizing paint slag collected in this way (for example, Japanese Patent Publication No. 52-35373), it is difficult to handle due to its high viscosity and strong adhesion, so it is not actually used effectively. The reality is that waste is disposed of by incineration or landfill. However, because the properties of slag are as described above, it takes a lot of effort to handle it for incineration or landfilling.In particular, when incinerating slag, it may soften and flow due to heat, causing abnormal combustion, or Combustion is extremely difficult to manage as it decomposes and releases harmful gases, requiring a special combustion furnace. The present invention provides a method for treating paint slag that turns such paint slag into spongy particles that are not sticky and do not soften or flow when heated, and the purpose is to make the paint slag into a form that is easy to handle. By doing so, it is possible to smoothly and economically collect and utilize the resources as effective resources. The term "sponge-like particles" as used in the present invention does not refer to particles having a sponge-like structure, but rather particles having a sponge-like feel.
The particles are individually irregular in shape, the particle size is not necessarily constant, and includes particles of aggregates of small particles, and the color is not specified. In order to make effective use of paint slag, it is necessary to make it easier to handle it, and as a result of experimenting to reduce the stickiness, we found that the stickiness easily disappears when alkali or acid is added and heated. There was found. It is thought that the loss of tackiness is due to the resin component of the paint slag being changed by the alkali or acid and curing is accelerated, but the reaction mechanism is not clear. When an alkali is added and heated and stirred, the paint slag generally becomes paste-like and does not harden significantly, although it varies depending on the type of paint slag, but when an acid is added, it changes to a sponge-like state containing coexisting water. However, although the particle size changes depending on the stirring conditions, the particles have approximately the same particle size. These particles have no stickiness or heat softening properties that paint slag has, so they can be easily transported and
It is easy to store, and can be used as a filler by drying and pulverizing, or can be processed by combustion without any problems. Therefore, it becomes possible to collect the paint slag and to utilize it smoothly and economically. As the strong acid, either mineral acid or organic acid can be used, but strong acids such as hydrochloric acid, sulfuric acid, and para-toluenesulfonic acid are suitable, with sulfuric acid being the most suitable in terms of availability, ease of handling, and price. . This acid can be used at a concentration that is generally commercially available, or in some cases, the waste acid that maintains strong acidity can be used as it is.
Or dilute with water and use. If the acid is diluted and added, it will contain more water and have better fluidity, making it easier to stir throughout the process. The amount of acid added is 1% or more based on the paint slag, but it is diluted by the 30 to 50% water content of the paint slag, so if the acid is diluted and added, the final acid concentration is 3%. It is desirable to adjust it so that it is more than that. If the temperature is below 50°C, curing will be slow, and if the temperature is above 90°C, the resin component will decompose and harmful gases such as formaldehyde and acrolein will be violently generated, so heating and stirring is preferably from 50 to 80°C. As the curing reaction progresses, the adhesive becomes sponge-like particles containing water and loses its stickiness. The size of the particles changes depending on the strength of stirring, and if stirring is performed such as applying a large shearing force or mixing and stirring such as grinding is performed, the particles become fine. If a small amount of surfactant is added during this curing reaction and the mixture is heated and stirred to cause slight foaming, the fluidity of the reactant increases and the stirring and mixing state becomes better. The surfactant may be anionic, cationic, or nonionic, but for example, dodecyltrimethylammonium chloride is added in an amount of 0.05 to 1% based on the paint slag. Stirring that causes significant foaming or excessive addition of surfactant is unfavorable in terms of operation since reactants overflow from the tank. The acid remaining in the acid-treated paint slag may be neutralized with an alkali such as sodium hydroxide, or it may be removed by washing with water. Since the coarse particles obtained by the treatment of the present invention as described above are non-adhesive particles, it is extremely easy to dispose of them as they are, and since they themselves contain considerable calories and valuable inorganic substances, By incineration, valuable materials can be recovered and used as a heat source. Therefore, the effects of the present invention are extremely large. Example 1 Paint slag (pigment 12%, thermosetting resin 48%, solvent 9
%, water 31%), 5 g of the acid shown in Table 1 and 25 g of water were added to 50 g, and the mixture was heated and stirred at 70 to 80°C. The results are shown in Table 1.

【表】【table】

【表】 実施例 2 15容のクラツチヤー型撹拌槽に塗料滓(顔料
8%、熱硬化性樹脂42%、溶剤5%、水5%)を
仕込み、硫酸および水を加えて加熱撹拌した。結
果を表2に示す。
[Table] Example 2 Paint slag (8% pigment, 42% thermosetting resin, 5% solvent, 5% water) was placed in a 15 volume crutcher-type stirring tank, sulfuric acid and water were added, and the mixture was heated and stirred. The results are shown in Table 2.

【表】 実施例 3 実施例2の実験番号No.3と同様の条件で界面活
性剤を添加した。結果を表3に示す。
[Table] Example 3 A surfactant was added under the same conditions as in Experiment No. 3 of Example 2. The results are shown in Table 3.

【表】【table】

【表】 実施例 4 6容のニーダー型捏加機に塗料滓(実施例1
に同じ)3.0Kgを仕込み、98%硫酸90gを加えて
加熱撹拌した。温度65〜70℃、撹拌回転数78r.p.
m.で15分反応し、40%水酸化ナトリウム200gを
用いて中和した。粒径0.2〜0.5mmの粒子3.2Kgを得
た。
[Table] Example 4 Paint slag (Example 1
(same as above) was charged, 90g of 98% sulfuric acid was added, and the mixture was heated and stirred. Temperature 65-70℃, stirring speed 78r.p.
m. for 15 minutes and neutralized using 200 g of 40% sodium hydroxide. 3.2 kg of particles with a particle size of 0.2-0.5 mm were obtained.

Claims (1)

【特許請求の範囲】 1 熱硬化性樹脂、顔料、溶剤等からなり、かつ
水分を含有する粘稠性の固形分50%以上の噴霧塗
装廃棄物に強酸を加え攪拌することにより該廃棄
物を非粘着性の粗粒物とすることを特徴とする塗
装廃棄物の処理方法。 2 強酸が硫酸、塩酸、硝酸、パラトルエンスル
ホン酸若しくはこれ等の使用ずみ強酸性廃酸であ
る特許請求の範囲第1項記載の処理方法。 3 酸の使用量が被処理塗装廃棄物に対し1〜15
重量%である特許請求の範囲第1項記載の処理方
法。 4 強酸が稀釈して使用される特許請求の範囲第
1項記載の処理方法。 5 攪拌処理が界面活性剤の存在下で行なわれる
特許請求の範囲第1項記載の処理方法。 6 攪拌処理が50〜90℃の加温下で行なわれる特
許請求の範囲第1項記載の処理方法。 7 粗粒化物が不整形でありスポンジ状の弾性を
も有する凝集体状のものを主とするものである特
許請求の範囲第1項に記載の処理方法。
[Claims] 1 A strong acid is added to viscous spray painting waste containing water and having a solid content of 50% or more, and the waste is then stirred. A method for treating painting waste, characterized by converting it into non-adhesive coarse particles. 2. The treatment method according to claim 1, wherein the strong acid is sulfuric acid, hydrochloric acid, nitric acid, para-toluenesulfonic acid, or a used strong acidic waste acid such as these. 3 The amount of acid used is 1 to 15% of the painted waste to be treated.
% by weight. The treatment method according to claim 1. 4. The treatment method according to claim 1, wherein the strong acid is used diluted. 5. The treatment method according to claim 1, wherein the stirring treatment is carried out in the presence of a surfactant. 6. The treatment method according to claim 1, wherein the stirring treatment is performed under heating at 50 to 90°C. 7. The treatment method according to claim 1, wherein the coarse grains are mainly aggregates that are irregularly shaped and have spongy elasticity.
JP59042375A 1984-03-06 1984-03-06 Treatment of coating waste Granted JPS60186546A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59042375A JPS60186546A (en) 1984-03-06 1984-03-06 Treatment of coating waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59042375A JPS60186546A (en) 1984-03-06 1984-03-06 Treatment of coating waste

Publications (2)

Publication Number Publication Date
JPS60186546A JPS60186546A (en) 1985-09-24
JPH0553828B2 true JPH0553828B2 (en) 1993-08-11

Family

ID=12634300

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59042375A Granted JPS60186546A (en) 1984-03-06 1984-03-06 Treatment of coating waste

Country Status (1)

Country Link
JP (1) JPS60186546A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3821760A1 (en) * 1988-06-28 1990-02-22 Kluthe Gmbh Chem Werke METHOD FOR RECOVERY OF PIGMENTS AND BINDING AGENTS FROM LACQUER COAGULATES
DE3821761A1 (en) * 1988-06-28 1990-02-22 Kluthe Gmbh Chem Werke METHOD FOR RECOVERY OF PIGMENTS, BINDING AGENTS AND SOLVENTS FROM RINSE DISCHARGERS SOILED WITH LACQUER

Also Published As

Publication number Publication date
JPS60186546A (en) 1985-09-24

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