JPS5831217B2 - Aeon Kokanjiyushino Shiyorihouhou - Google Patents

Aeon Kokanjiyushino Shiyorihouhou

Info

Publication number
JPS5831217B2
JPS5831217B2 JP49019213A JP1921374A JPS5831217B2 JP S5831217 B2 JPS5831217 B2 JP S5831217B2 JP 49019213 A JP49019213 A JP 49019213A JP 1921374 A JP1921374 A JP 1921374A JP S5831217 B2 JPS5831217 B2 JP S5831217B2
Authority
JP
Japan
Prior art keywords
water
exchange resin
cation exchange
paint
resin
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
Application number
JP49019213A
Other languages
Japanese (ja)
Other versions
JPS50113481A (en
Inventor
敬 砂盛
英樹 児嶋
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.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP49019213A priority Critical patent/JPS5831217B2/en
Publication of JPS50113481A publication Critical patent/JPS50113481A/ja
Publication of JPS5831217B2 publication Critical patent/JPS5831217B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は陽イオン交換樹脂の処理方法、特に酸性基を含
有する樹脂の中和物を主体とする濃厚塗料を吸着した陽
イオン交換樹脂より濃厚塗料を回収再使用すると共に、
洗浄処理した陽イオン交換樹脂を再生処理することを特
徴とするイオン交換樹脂の処理方法に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating a cation exchange resin, and in particular, to recovering and reusing a concentrated paint from a cation exchange resin that has adsorbed a concentrated paint mainly composed of a neutralized product of a resin containing acidic groups. With,
The present invention relates to a method for treating an ion exchange resin, which comprises regenerating a washed cation exchange resin.

近年、公害問題発生の防止、或いは塗装工程の合理化な
どを目的とした場合、水性塗料を用いる方法が、従来の
有機溶剤系塗料を用いる方法に比べて有利なことが注目
を集めている。
In recent years, methods using water-based paints have attracted attention for their advantages over conventional methods using organic solvent-based paints for the purpose of preventing pollution problems or streamlining the painting process.

しかし現在まで開発されてきた水性塗料は塗料を構成す
る樹脂中に含まれる極性の強い低分子物質が含まれてお
り、このような塗料を水で稀釈し水性塗料浴を形成せし
める場合には水性塗料浴を構成している塗料粒子より上
記極性の強い低分子化合物が経時的に水性媒体中に溶出
し、塗料粒子の水性媒体中での分散安定平衡をみだし、
塗料粒子の分散安定性を損っていた。
However, the water-based paints that have been developed to date contain highly polar low-molecular substances contained in the resin that makes up the paint. The above-mentioned highly polar low-molecular compounds are eluted into the aqueous medium over time from the paint particles constituting the paint bath, creating a stable dispersion equilibrium of the paint particles in the aqueous medium.
The dispersion stability of paint particles was impaired.

また上述した如き酸性基を有する樹脂を中和して水性塗
料を作った場合、特に水性塗料浴を用いた浸漬塗装、或
いは電着塗装に於ては被塗物に塗装された塗膜中に含ま
れる塩基の量と補給塗料中に含まれる塩基の量とは一致
せず常に塗膜となって水性塗料浴から持出されてゆく塩
基の方が常に少ないため、塗装の進行に伴って水性塗料
浴中には過剰の塩基が蓄積され、水性塗装浴の特性、或
いは、このような水性塗装浴を用いて塗装された塗装品
の塗膜の特性が低下する傾向を示すため、水性塗装浴を
常に陽イオン交換樹脂で処理し、水性塗装浴中の塩基の
濃度を一定に保つような手法が開発されているが、この
ような手法では、その操作が煩雑とならざるを得ない。
In addition, when water-based paints are made by neutralizing resins with acidic groups such as those mentioned above, especially in dip coating using a water-based paint bath or electrodeposition coating, there may be The amount of base contained in the paint does not match the amount of base contained in the replenishment paint, and the amount of base that is always carried out as a coating film from the water-based paint bath is always smaller. Water-based paint baths should not be used because excessive bases tend to accumulate in paint baths and deteriorate the properties of the water-based paint bath or the properties of the coatings of coated articles painted using such water-based paint baths. A method has been developed in which the base concentration in the aqueous coating bath is kept constant by constantly treating the base with a cation exchange resin, but such a method inevitably requires complicated operations.

そこでこのような煩雑な操作が必要のない水性塗料の製
造法について本発明者等は検討を加え、酸基を有する樹
脂又はその中和物を陰イオン交換樹脂処理し、続いて必
要により中和剤を加えた後、この樹脂を更に陽イオン交
換樹脂で処理する方法の技術を確立し先に特許出願した
Therefore, the present inventors investigated a method for producing water-based paints that does not require such complicated operations, and treated a resin having an acid group or its neutralized product with an anion exchange resin, and then neutralized it if necessary. After adding the agent, we have established a technology for further treating this resin with a cation exchange resin, and have previously applied for a patent.

こSで問題となってきたのは酸性基含有樹脂の中和物を
陽イオン交換樹脂で処理し、更に陽イオン交換樹脂を再
生処理しようとした場合、陽イオン交換樹脂に吸着され
た濃厚塗料の取扱いである。
The problem with this S is that when a neutralized product of an acidic group-containing resin is treated with a cation exchange resin and the cation exchange resin is further regenerated, the concentrated paint adsorbed on the cation exchange resin This is the handling of

これは通常の方法によって水洗すれば容易に除去するこ
とはできるのであるが、この洗浄水をそのま5廃液とす
る場合には廃水自体が公害発生の原因となり大きな社会
問題となるのであるが、それよりも、この陽イオン交換
樹脂に吸着された濃厚塗料は、それ自体塗料として用い
た場合、伺等問題なく利用しうるのであり、この濃厚塗
料をいかにうまく回収するのかにある。
This can be easily removed by washing with water using normal methods, but if this washing water is used directly as waste water, the waste water itself becomes a cause of pollution and becomes a major social problem. Rather, if the concentrated paint adsorbed on the cation exchange resin is itself used as a paint, it can be used without any problems, and the problem lies in how well this concentrated paint can be recovered.

そこで本発明者等は、上記問題を解決するべく検討しこ
の濃厚塗料の効率的な回収方法について検討し本発明を
完成した。
In order to solve the above problems, the present inventors investigated an efficient method for recovering this thick paint, and completed the present invention.

本発明の要旨とするところは酸基含有樹脂の中和物を吸
着した陽イオン交換樹脂を脱イオン水、前記酸基含有樹
脂の中和物の陽イオン交換樹脂処理を施した樹脂を用い
て作られた水性塗料浴、或いはこの水性塗料浴を用い電
着塗装した塗装品の脱イオン水による洗浄廃液又は、こ
れらを超限外濾過器若しくは逆浸透圧濾過器を通すこと
によって得られた水で洗浄すると共にこの洗浄水を前記
水性塗料浴にもとすか、或いはこの洗浄水を酸性基含有
樹脂の中和物を稀釈し水性塗料浴を形成する際の稀釈溶
媒として用いると共に、洗浄処理の終了した陽イオン交
換樹脂を必要により更に水洗した後再生処理することを
特徴とする陽イオン交換樹脂の処理方法にある。
The gist of the present invention is to use a cation exchange resin that has adsorbed a neutralized product of an acid group-containing resin, deionized water, and a resin that has been treated with a cation exchange resin that has adsorbed a neutralized product of the acid group-containing resin. A water-based paint bath made, or waste liquid from washing with deionized water of painted products electrodeposited using this water-based paint bath, or water obtained by passing these through an ultra-ultrafilter or a reverse osmosis filter. or use this washing water as a dilution solvent when diluting the neutralized product of the acidic group-containing resin to form an aqueous paint bath. A method for treating a cation exchange resin, which is characterized in that the finished cation exchange resin is further washed with water if necessary, and then regenerated.

本発明の方法によると従来法の如く濃厚塗料を吸着した
陽イオン交換樹脂の塗料の除去に際し、水道水や工業用
水を用いることがないため回収した塗料含有水をそのま
\、水性塗料浴へもどしても、或いはこの回収水を塗料
の稀釈溶媒の一部として用い水性塗料浴を作っても塗料
の浴安定性を低下せしめるような猥雑イオンが含まれて
いないため、塗料の稀釈溶媒として脱イオン水を用いて
作られた水性塗料浴の安定性に比べ伺等損色のない水性
塗料浴とすることができる。
According to the method of the present invention, unlike conventional methods, tap water or industrial water is not used when removing paint from a cation exchange resin that has adsorbed concentrated paint, so the recovered paint-containing water is directly transferred to the aqueous paint bath. Even if the recovered water is recovered or used as part of the paint dilution solvent to make an aqueous paint bath, it does not contain any obscene ions that would reduce the bath stability of the paint. Compared to the stability of water-based paint baths made using ionized water, it is possible to create a water-based paint bath that does not cause color loss.

また処理する陽イオン樹脂も、外部からの猥雑イオンの
吸着を極めて効率よく防止することができ極めて好都合
な方法である。
Furthermore, the cationic resin to be treated can also very efficiently prevent the adsorption of obscene ions from the outside, making this an extremely convenient method.

本発明の方法が最も効率よくその効果を発揮するのは、
酸性基を含有する樹脂又はその中和物を陰イオン交換樹
脂で処理し、酸基含有樹脂中に含まれる極性の強い酸性
物質、特に酸性を示す単量体の未重合物、或いはそれら
の低重合物、又は重合触媒、使用単量体中に含まれるハ
イドロキノンの如さ安定剤の分解物などの塗料の水性媒
体中での分散安定性を低下せしめたり、これらの水性塗
料より形成された塗膜の加熱硬化時に於けるヒートリフ
ロウ性を低下せしめると共に得られる塗膜の耐蝕性、耐
水性などを低下せしめる物質を除去した酸性基含有樹脂
の中和物を吸着した陽イオン変装樹脂の処理に適用した
場合であり、本発明の方法によると濃厚塗料を吸着した
陽イオン交換樹脂の処理ははゾ閉サイクルで処理するこ
とができるため廃水による公害発生問題もなく、また回
収した塗料の有効利用ができる点が大きな利点である。
The method of the present invention exhibits its effects most efficiently because:
Acidic group-containing resin or its neutralized product is treated with an anion exchange resin to remove highly polar acidic substances contained in the acidic group-containing resin, especially unpolymerized monomers exhibiting acidity, or their reduced Polymerization products, polymerization catalysts, decomposition products of stabilizers such as hydroquinone contained in the monomers used, etc. may reduce the dispersion stability of paints in aqueous media, and coatings formed from these water-based paints may Applicable to the treatment of cationic disguised resins that have adsorbed neutralized products of acidic group-containing resins from which substances that reduce the heat reflow properties during heat curing of films and reduce the corrosion resistance and water resistance of the resulting coating films are removed. According to the method of the present invention, the cation exchange resin that has adsorbed concentrated paint can be treated in a closed cycle, so there is no problem of pollution caused by wastewater, and the recovered paint can be used effectively. The big advantage is that you can.

実施例 撹拌器、還流コンデンサー及び温度計を備えたフラスコ
中に2−エチルへキシルアクリレート39.9部、スチ
レン25.8部、N−ブトキシメチルアクリルアミド1
9.1部、イタコン酸3.23部、アゾビスイソブチロ
ニトリル2.93部、2−メルカプトエタノール1.1
2部、イソプロピルアルコール62,5部を仕込み2時
間30分かけて70’Cに昇温し、続いて70℃で5時
間30分重合を続けた。
Example In a flask equipped with a stirrer, a reflux condenser and a thermometer, 39.9 parts of 2-ethylhexyl acrylate, 25.8 parts of styrene, and 1 part of N-butoxymethylacrylamide were added.
9.1 parts, itaconic acid 3.23 parts, azobisisobutyronitrile 2.93 parts, 2-mercaptoethanol 1.1
2 parts and 62.5 parts of isopropyl alcohol were charged, the temperature was raised to 70'C over 2 hours and 30 minutes, and then polymerization was continued at 70C for 5 hours and 30 minutes.

その後75℃に昇温し4時間そのま\の状態に保つこと
によって重合を終了した。
Thereafter, the temperature was raised to 75°C and the temperature was maintained for 4 hours to complete the polymerization.

上記の如くして得た酸性樹脂の溶液に全カルボキシル基
の45%に相当する量のβ−ジメチルアミンエタノール
を加えることによって樹脂を中和した。
The resin was neutralized by adding β-dimethylamine ethanol in an amount corresponding to 45% of the total carboxyl groups to the acidic resin solution obtained as described above.

この中和樹脂溶液100部に対し酸化チタン75部(帝
国化手製:JR−600E)を加えボールミルでよく混
練しさらに上記の中和樹脂溶液200部を加えることに
よって白色エナメルペースト囚を作った。
To 100 parts of this neutralized resin solution, 75 parts of titanium oxide (JR-600E, manufactured by Teikoku Kaisha Ltd.) was added, thoroughly kneaded in a ball mill, and then 200 parts of the above neutralized resin solution was added to prepare a white enamel paste.

白色エナメルペースト(Al 1 kyに対し脱イオン
水5(Bi’を加え更に200メツシユのOH型陰イオ
ン交換樹脂5g(三菱化成工業株式会社製ダイヤイオン
5A−2OA)を加え、よく撹拌した後、イオン交換樹
脂をフィルターによって取除き白色エナメルペースト■
を作った。
After adding 5 g of deionized water (Bi' to 1 ky of white enamel paste) and 5 g of 200 mesh OH type anion exchange resin (Diaion 5A-2OA manufactured by Mitsubishi Chemical Corporation) and stirring well, The ion exchange resin is removed by a filter and white enamel paste is created.■
made.

白色エナメルペースト■をH型強酸型陽イオン交換樹脂
(三菱化成工業株式会社製ダイヤイオンWK−10)充
填塔を通すことによって白色エナメルペーストoを作っ
た。
A white enamel paste O was prepared by passing the white enamel paste (1) through a column packed with an H-type strong acid type cation exchange resin (Diaion WK-10 manufactured by Mitsubishi Chemical Industries, Ltd.).

このようにして陽イオン交換樹脂を吸着した白色エナメ
ルペースKCIIを脱イオン水で洗浄したものを洗浄液
CI’)とし、また白色エナメルペースト0を固形分濃
度が約15重量%になるように調整した電着塗装浴を超
限外濾過器を通すことによって得られた水で洗浄したも
のを洗浄液印とし、更に上記電着塗装浴を用いて電着塗
装した塗装品を脱イオン水で洗浄した洗浄水で洗浄した
ものを洗浄液(9)とした。
The white enamel paste KCII that had adsorbed the cation exchange resin in this way was washed with deionized water and used as a cleaning solution CI'), and the white enamel paste 0 was adjusted to have a solid content concentration of about 15% by weight. The cleaning liquid mark is obtained by washing the electrodeposition coating bath with water obtained by passing it through an ultra-ultrafilter, and further washing the painted product electrodeposited using the above electrodeposition coating bath with deionized water. What was washed with water was used as a washing liquid (9).

更に上記電着塗装浴で上記イオン交換樹脂充填塔を洗浄
した洗浄水を洗浄水■とした。
Furthermore, the washing water used to wash the ion exchange resin packed tower with the electrodeposition coating bath was designated as washing water (2).

また白色エナメルペースト(Alを上記方法で用いたも
のと同様の陽イオン交換樹脂充填塔を通し後、この陽イ
オン交換樹脂充填塔を脱イオン水で洗浄し、この回収液
を洗浄液間とした。
In addition, the white enamel paste (Al) was passed through a cation exchange resin packed tower similar to that used in the above method, and then the cation exchange resin packed tower was washed with deionized water, and the recovered liquid was used as a cleaning solution.

上述の如くして得た洗浄水(7)を濃縮又は白色エナメ
ルペースト■を加えることによって固形分濃度約15重
量%とし電着塗装浴を調整すると共に、白色エナメルペ
ーストIC)を脱イオン水で固形分濃度が15重量%に
なるように調整し電着塗装浴を調整した。
The washing water (7) obtained as described above was concentrated or added with white enamel paste (2) to a solid content of about 15% by weight to prepare an electrodeposition coating bath, and the white enamel paste (IC) was added with deionized water. An electrodeposition coating bath was prepared by adjusting the solid content concentration to 15% by weight.

上述の如くして調整した電着塗装浴を用い、被塗物とし
てリン酸亜鉛処理板を用い、電圧120v1電着時間2
分とし、得られた塗装品を水洗后180℃で30分間焼
付けることによって形成された塗膜の特性並びに各電着
塗装浴の特性を次表に示した。
Using the electrodeposition coating bath prepared as described above, using a zinc phosphate treated plate as the object to be coated, voltage 120v1 electrodeposition time 2
The properties of the coating film formed by washing the obtained coated product with water and baking it at 180° C. for 30 minutes, as well as the properties of each electrodeposition coating bath, are shown in the following table.

上表の結果からも明らかな如く本発明の方法によって回
収された塗料は何等白色エナメルペースト圓に損色ない
用いうることか分る。
As is clear from the results in the table above, it can be seen that the paint recovered by the method of the present invention can be used in white enamel paste circles without color loss.

また、洗浄を終了したイオン交換樹脂は、吸着していた
樹脂分かはゾ完全に取除かれたのでその再生処理は極め
て容易であった。
In addition, after washing the ion exchange resin, the adsorbed resin content was completely removed, so the regeneration process was extremely easy.

Claims (1)

【特許請求の範囲】[Claims] 1 酸基含有樹脂の中和物を吸着した粒径1200μ以
下の陽イオン交換樹脂を脱イオン水、前記酸基含有樹脂
の中和物を用いて作られた水性塗料浴、或いはこの水性
塗料浴を用い電着塗装を行った塗装品の脱イオン水によ
る水洗廃水、または前記水性塗料浴、水洗廃水を超眼外
沢過装置または逆浸透濾過器を通すことによって得られ
た水で洗浄し、この洗浄水を前記水性塗料浴にもどすか
、又は、酸性基含有樹脂の中和物を稀釈し水性塗料浴を
形成せしめる際の稀釈溶媒として用いると共に、洗浄処
理を終了した陽イオン交換樹脂を再生処理することを特
徴とする陽イオン交換樹脂の処理方法。
1. A water-based paint bath made by using a cation exchange resin with a particle size of 1200μ or less that has adsorbed a neutralized product of an acid group-containing resin, deionized water, and a neutralized product of the acid group-containing resin, or this water-based paint bath. washing wastewater with deionized water of a coated product that has been electrodeposited using the method, or washing the water-based paint bath or washing wastewater with water obtained by passing it through a super extraocular filtration device or a reverse osmosis filter, This washing water is returned to the aqueous paint bath or used as a diluting solvent when diluting the neutralized product of the acidic group-containing resin to form an aqueous paint bath, and the cation exchange resin after the washing process is recycled. 1. A method for treating a cation exchange resin, the method comprising: treating a cation exchange resin;
JP49019213A 1974-02-18 1974-02-18 Aeon Kokanjiyushino Shiyorihouhou Expired JPS5831217B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP49019213A JPS5831217B2 (en) 1974-02-18 1974-02-18 Aeon Kokanjiyushino Shiyorihouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP49019213A JPS5831217B2 (en) 1974-02-18 1974-02-18 Aeon Kokanjiyushino Shiyorihouhou

Publications (2)

Publication Number Publication Date
JPS50113481A JPS50113481A (en) 1975-09-05
JPS5831217B2 true JPS5831217B2 (en) 1983-07-05

Family

ID=11993080

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49019213A Expired JPS5831217B2 (en) 1974-02-18 1974-02-18 Aeon Kokanjiyushino Shiyorihouhou

Country Status (1)

Country Link
JP (1) JPS5831217B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5322546A (en) * 1976-08-13 1978-03-02 Nippon Giken Kk Method of washing resin in apparatus for refining electrodeposition paint
JPS5485229A (en) * 1977-12-20 1979-07-06 Fuji Satsushi Kogyo Kk Treatment of electrodepositing coating waste solution
JP2540186Y2 (en) * 1991-02-19 1997-07-02 積水ハウス株式会社 Outside staircase

Also Published As

Publication number Publication date
JPS50113481A (en) 1975-09-05

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