JPS6054352B2 - Aqueous coating composition - Google Patents
Aqueous coating compositionInfo
- Publication number
- JPS6054352B2 JPS6054352B2 JP3081078A JP3081078A JPS6054352B2 JP S6054352 B2 JPS6054352 B2 JP S6054352B2 JP 3081078 A JP3081078 A JP 3081078A JP 3081078 A JP3081078 A JP 3081078A JP S6054352 B2 JPS6054352 B2 JP S6054352B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- polybutadiene
- mercaptan
- sample
- reaction
- 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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- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
【発明の詳細な説明】
本発明は新規な水性被覆用組成物に関し、さらに詳し
くは、塗膜の耐食性、耐水性、硬度などにおいてすぐれ
た性能を示す新規な水性被覆用組成物に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel aqueous coating composition, and more particularly to a novel aqueous coating composition that exhibits excellent performance in coating film corrosion resistance, water resistance, hardness, and the like.
従来、水性塗料用のビヒクルとしては天然乾性油のマ
レイン化物、エポキシエステル樹脂、マレイン化ポリブ
タジエン等が用いられている。Conventionally, maleated natural drying oils, epoxy ester resins, maleated polybutadiene, and the like have been used as vehicles for water-based paints.
これらは通常アンモニア、アミン、苛性カリなどの塩基
て中和して水溶化または水分散化されて用いられるが、
電着塗装の場合にはこれらの樹脂が陽極に接続された被
塗物上に析出される。 しかしながら、このような陽極
析出電着塗装法にはいくつかの基本的な問題点があり、
近年のきびしい耐食性の要求に充分満足出来る方法とは
言えない。These are usually used after being neutralized with a base such as ammonia, amine, or caustic potash to make them water-soluble or water-dispersed.
In the case of electrodeposition coating, these resins are deposited on the object connected to the anode. However, there are some basic problems with this anodic electrodeposition coating method.
This cannot be said to be a method that fully satisfies recent demands for severe corrosion resistance.
即ち、陽極析出電着塗装の場合には被塗物金属が陽極て
あるため電着塗装時にイオン化され金属素地や化成皮膜
の溶出を伴い、また析出塗膜中に一部残留した金属イオ
ンは塗膜を着色させ塗膜の耐食性、耐アルカリ性を損い
やすい。これに対して陰極析出電着塗装の場合には、金
属の溶出あるいは化成皮膜の溶出が起らないため着色が
なく、耐食性、耐アルカリ性などの面ても優れた塗膜が
用いられる。 この陰極析出電着塗装に用いられる樹脂
については従来から種々検討がなされており、例えばエ
ポキシ基へのアミン付加反応を利用した変性エポキシ樹
脂(特公昭49−23807号、特公昭49−3173
6号)、塩基性アミノ基をもつ不飽和化合物をラジカル
共重合させた変性アクリル樹脂(特公昭48一3714
7号など)、酸無水物基とジアミンとの反応によるイミ
ノアミン含有樹脂(特開昭51−119727号)等が
提案されている。In other words, in the case of anodic deposition electrodeposition coating, since the metal to be coated is an anode, it is ionized during electrodeposition coating, and the metal base and chemical conversion coating are eluted, and some of the metal ions remaining in the deposited coating film are removed from the coating. It tends to color the film and impair the corrosion resistance and alkali resistance of the paint film. On the other hand, in the case of cathodic deposition electrodeposition coating, there is no elution of metal or chemical conversion film, so there is no coloration, and a coating film that is excellent in terms of corrosion resistance, alkali resistance, etc. is used. Various studies have been conducted on the resins used in this cathodic electrodeposition coating.
No. 6), a modified acrylic resin made by radical copolymerization of an unsaturated compound having a basic amino group (Japanese Patent Publication No. 48-3714
No. 7), iminoamine-containing resins produced by the reaction of acid anhydride groups with diamines (Japanese Patent Application Laid-Open No. 119727/1983), and the like have been proposed.
しかしながら、これらの陰極析出樹脂を用いた塗膜は
、一般に硬化温度が高い、浴塗料の電導度が低いためつ
きまわり性が悪い、希釈塗料の安定性が悪い、さらには
原料コストがいちじるしく高い等の欠点があり、末だ広
く実用化されるには至つていない。However, coating films using these cathodically deposited resins generally have high curing temperatures, poor throwing power due to low conductivity of bath paints, poor stability of diluted paints, and significantly high raw material costs. However, it has several drawbacks and has not been widely put into practical use.
また陽極析出型電着塗料の場合には、塗膜の性能を向上
させる為にメラミン樹脂やフェノール樹脂の併用がしば
しば行なわれているが、陰極析出型塗料の場合には、樹
脂中に存在する塩基性のアミノ基のため酸性側で硬化が
促進される性質をもつメラミン樹脂やフェノール樹脂等
を添加しても硬化反応が充分に行なわれない恐れがあり
、そのため十分な硬化性をもつことが要求される。本発
明の目的は、陰極析出型電着塗料として具備すべきかか
る諸機能を有し、かつ耐衝撃性、硬度等の機械的強度な
らびに耐水性、耐食性等の化学的諸性質の優れた塗膜を
賦与することの出来る被覆用組成物を提供することにあ
る。In addition, in the case of anodic deposition type electrodeposition paints, melamine resins and phenolic resins are often used in combination to improve the performance of the coating film, but in the case of cathodic deposition type paints, melamine resins and phenolic resins are often used in combination with the resin. Even if you add melamine resin, phenol resin, etc., which have basic amino groups and have the property of accelerating curing on the acidic side, the curing reaction may not be carried out sufficiently, so it is difficult to have sufficient curing properties. required. The object of the present invention is to provide a coating film that has the various functions that a cathodic deposition type electrodeposition coating should have, and that has excellent mechanical strength such as impact resistance and hardness, and chemical properties such as water resistance and corrosion resistance. The object of the present invention is to provide a coating composition that can impart the following properties.
本発明のこれらの目的は、液状ポリブタジエンの二重結
合に対してメルカプト基を含有する有機化合物を部分的
に附加せしめ、生じたメルカプタン変性ポリブタジエン
を少なくとも部分的にスルホニウムイオン化することに
より得られる水溶性または水分散性樹脂を水希釈性被覆
用組成物のビヒクル成分として使用することによつて達
成される。These objects of the present invention are to partially add an organic compound containing a mercapto group to the double bonds of liquid polybutadiene, and to ionize the resulting mercaptan-modified polybutadiene at least partially with sulfonium. or by using a water-dispersible resin as a vehicle component of a water-dilutable coating composition.
本発明において使用される液状ポリブタジエンは、50
0〜50001好ましくは700〜4000の数平均分
子量、100〜5001好ましくは150〜480のヨ
ウ素価、40%以上、好ましくは50%以上の1.4一
結合を有するものであればいずれでもよく、その末端は
非官能性でも水酸基やカルボキシル基がついたものでも
どちらでもよい。The liquid polybutadiene used in the present invention is 50
Any compound having a number average molecular weight of 0 to 50,001, preferably 700 to 4,000, an iodine value of 100 to 5,001, preferably 150 to 480, and a 1.4 bond of 40% or more, preferably 50% or more, may be used. The terminal may be non-functional or may have a hydroxyl or carboxyl group.
しかし、分子量が50昧満であると得られる塗膜の乾燥
性や機械物性がいちじるしく低下し、また分子量が50
0より大きい場合にはメルカプタン化合物の附加反応時
においてゲル化が起こりやすく、また水溶性が低下して
平滑な塗膜が得られない。However, if the molecular weight is less than 50, the drying properties and mechanical properties of the resulting coating film will be significantly reduced;
When it is larger than 0, gelation tends to occur during the addition reaction of the mercaptan compound, and water solubility decreases, making it impossible to obtain a smooth coating film.
ヨウ素価があまり小さい場合には空気硬化性が悪く、逆
に大きすぎる場合には塗膜の耐候性や機械物性が損われ
る。一方、1.4一結合が40%未満のポリブタジエン
の場合は、メルカプタン化合物を附加せしめる際にゲル
を生じやすく、かつまた得られた塗膜の耐食性において
きわめて乏しい結果しか得られない。液状ポリブタジエ
ンとメルカプタン化合物との附加反応は、たとえばケミ
カル・リアクシヨンズ●オブ●ポリマーズ(Chemi
calReactiOnsOfPOlyTners)第
133頁〔インターサイエンス パブリツシヤーズ(I
ntersciencePubIishers)、ハイ
●ポリマー●シリーズ(HighPOlymerSer
ies)第用巻196祥発行〕に記されているように、
ゴム状高分子物質に対して一般に行われるような条件下
で実施すればよく、代表的にはベンゼン、トルエン、キ
シレンのような不活性溶剤及び過酸化物やアゾビスイソ
ブチロニトリルのような触媒の存在下に50〜200℃
で実施される。If the iodine value is too low, air curing properties will be poor, and if it is too high, the weather resistance and mechanical properties of the coating will be impaired. On the other hand, in the case of polybutadiene having less than 40% of 1.4 bonds, gels tend to form when a mercaptan compound is added, and the corrosion resistance of the resulting coating film is extremely poor. Addition reactions between liquid polybutadiene and mercaptan compounds are carried out by, for example, Chemical Reactions ● of ● Polymers (Chemi
calReactiOnsOfPOlyTners) page 133 [Interscience Publishers (I
tersciencePubIishers), High Polymer Series (HighPOlymerSer
ies) Volume 196, published],
It may be carried out under conditions commonly used for rubbery polymeric materials, typically using an inert solvent such as benzene, toluene, or xylene, and a peroxide or azobisisobutyronitrile. 50-200℃ in the presence of catalyst
It will be carried out in
また酸触媒の存在下て実施することもできるが、環化に
より必要以上に二重結合が消費されて塗料の硬化に不適
となつたり、生成物の精製がはん雑となるなどの難があ
る。本発明において用いられるメルカプタン化合物の例
としては、例えばa)メチルメルカプタン、プロピルメ
ルカプタン、ブチルメルカプタン、オクチルメルカプタ
ン、ドデシルメルカプタンのようなアルキルメルカプタ
ン、b)2−メルカプトエタノール、3−メルカプ目.
2−プロパンジオール、システイン、メルカプトフェノ
ール、メルカプトナフトールのような水酸基やフェノー
ル性水酸基を有するメルカプタン、c)2−アミノエチ
ルメルカプタン、メルカプトアニリンのような第一級な
いし第二級のアミノ基を有するメルカプタン、d)チオ
グリコール酸、メルカプトコハク酸、β−メルカプトプ
ロピオン酸、メルカプト安息香酸のようなりルボキシル
基含有メルカプタンなどがあげられ、なかでも炭素数1
2J:).下のものが賞用される。It can also be carried out in the presence of an acid catalyst, but there are problems such as the cyclization consumes more double bonds than necessary, making it unsuitable for curing the paint, and making the purification of the product complicated. be. Examples of mercaptan compounds used in the present invention include a) alkyl mercaptans such as methyl mercaptan, propyl mercaptan, butyl mercaptan, octyl mercaptan, and dodecyl mercaptan; b) 2-mercaptoethanol and 3-mercaptans.
Mercaptans having a hydroxyl group or phenolic hydroxyl group such as 2-propanediol, cysteine, mercaptophenol, and mercaptonaphthol; c) Mercaptans having a primary or secondary amino group such as 2-aminoethylmercaptan and mercaptoaniline; , d) Mercaptans containing a ruboxy group, such as thioglycolic acid, mercaptosuccinic acid, β-mercaptopropionic acid, and mercaptobenzoic acid, among which mercaptans containing a carbon number of 1
2J:). The one below will be awarded.
反応に使用されるメルカプタン化合物の量は、メルカプ
タン変性ポリブタジエンをスルホニウムイオン化したと
きに該メルカプタン変性ポリブタジエンを水に可溶化ま
たは分散化するのに十分な量であればよく、具体的には
メルカプタン変性ポリブタジエン中の硫黄分が1.5〜
25重量%、好ましくは2〜2唾量%となるような量で
ある。The amount of the mercaptan compound used in the reaction may be sufficient to solubilize or disperse the mercaptan-modified polybutadiene in water when the mercaptan-modified polybutadiene is sulfonium ionized. The sulfur content inside is 1.5~
The amount is 25% by weight, preferably 2 to 2% by weight.
この反応に際して反応混合物の粘度を下げ、反応を容易
にするために、溶剤を加えてもよいが、その場合には反
応終了後に減圧または抽出によつて未反応のメルカプタ
ン化合物や溶剤を留去するのが好ましい。メルカプタン
変性ポリブタジエンは、分子中にスルフィド結合の形で
含まれる硫黄原子を常法に従つてスルホニウムイオン化
することにより水溶化または水分散化される。During this reaction, a solvent may be added to reduce the viscosity of the reaction mixture and facilitate the reaction, but in that case, after the reaction is complete, unreacted mercaptan compounds and solvent are distilled off by vacuum or extraction. is preferable. Mercaptan-modified polybutadiene is made water-soluble or water-dispersible by ionizing the sulfur atoms contained in the molecule in the form of sulfide bonds with sulfonium according to a conventional method.
スルホニウムイオン化する方法としては、例えは蟻酸、
酢酸、プロピオン酸、酪酸、乳酸、ヒドロキシ酢酸、塩
酸、リン酸のような有機酸または無機酸及びエチレンオ
キサイド、プロピレンオキサイド、エピクロルヒドリン
、アリルグリシジルエーテルなどのようなエポキシ化合
物の共存下に処理する方法、スルフィドのスルホニウム
イオン化剤として公知のメチルクロライド、エチルクロ
ライド、ベンジルクロライドなどのようなハロゲン化ア
ルキルで処理する方法などがある。これらの処理剤の使
用量は、少くとも樹脂を水に可溶化または分散化させる
のに必要な量以上であればよく、スルフィド基の当量以
下であることが好ましい。この際、生成した水性樹脂を
含む系のPH2〜9、好ましくは3〜7とするのが適切
である。このようにして水溶性または水分散性にしたメ
ルカプタン変性重合体を、通常5〜6呼量%の水溶液ま
たは水分散液として水性被覆用組成物が調整されるが、
この組成物を水性塗料として用いる場合には、チタン白
、ストロンチウムクロメート、カーボンブラックなどの
ごとき通常の顔料を樹脂分10呼量部当り40鍾量部以
下の範囲で混合することが適切であり、その他所望によ
り老化防止剤、充填剤などを配合することもてきる。Examples of methods for ionizing sulfonium include formic acid,
A method of treating in the presence of an organic or inorganic acid such as acetic acid, propionic acid, butyric acid, lactic acid, hydroxyacetic acid, hydrochloric acid, phosphoric acid and an epoxy compound such as ethylene oxide, propylene oxide, epichlorohydrin, allyl glycidyl ether, etc. There is a method of treating sulfide with an alkyl halide such as methyl chloride, ethyl chloride, benzyl chloride, etc., which are known as sulfonium ionizing agents. The amount of these treatment agents used may be at least the amount necessary to solubilize or disperse the resin in water, and preferably not more than the equivalent amount of the sulfide group. At this time, it is appropriate that the pH of the system containing the produced aqueous resin be 2 to 9, preferably 3 to 7. The mercaptan-modified polymer thus made water-soluble or water-dispersible is usually prepared as an aqueous solution or dispersion of 5 to 6% by volume, but an aqueous coating composition is prepared.
When this composition is used as a water-based paint, it is appropriate to mix a common pigment such as titanium white, strontium chromate, carbon black, etc. in an amount of 40 parts by weight or less per 10 parts by weight of the resin. In addition, anti-aging agents, fillers, etc. may be added if desired.
もちろん、他の水溶性樹脂と併用することもてきる。ま
た、このようにして得られる水性塗料を常温または焼付
けによつて硬化させる刷毛塗りまたはスプレー塗装用に
使用する場合には、コバルト、鉛、マンガンなどの金属
石鹸をドライヤーとして配合することが適切てあり、電
着塗装用に用いる場合には、所望によりメラミン樹脂、
フェノール樹脂、エポキシ樹脂などの熱硬化型水溶性樹
脂を混合することもできる。以下に実施例を挙けて本発
明をさらに具体的に説明する。Of course, it can also be used in combination with other water-soluble resins. In addition, when using the water-based paint obtained in this way for brush painting or spray painting, which is cured at room temperature or by baking, it is appropriate to mix metal soaps such as cobalt, lead, and manganese as a dryer. When used for electrodeposition coating, melamine resin,
Thermosetting water-soluble resins such as phenol resins and epoxy resins can also be mixed. The present invention will be explained in more detail below with reference to Examples.
なお実施例及び参考例中の部及び%はすべて重量規準で
ある。参考例
試料A
触媒としてコバルrオクトエートージエチルアルミニウ
ムクロリドー水一亜燐酸トリフェニルを用い、ベンゼン
溶液中で30℃にて1.3−ブタジエンを重合して得た
液状ポリブタジエン(数平均分子量1100125℃に
おける粘度800センチポイズ、赤外吸収スペクトルに
よるシスー1A型結合含量53%、トランスー1.櫻結
合含量9%、および1.2型結合含量羽%)2(1)部
、2−アミノエチルメルカプタン6娼、キシレン3娼、
シターシヤリィブチルパーオキシド3部の混合物を14
0℃に加熱し、環流下に4時間反応させたのち、溶剤を
減圧下に除去することにより反応生成物258部を得た
。Note that all parts and percentages in Examples and Reference Examples are based on weight. Reference Example Sample A Liquid polybutadiene (number average molecular weight: 1100125 Viscosity at °C 800 centipoise, cis-1A bond content by infrared absorption spectrum 53%, trans-1.Sakura bond content 9%, and 1.2-type bond content (%) 2 (1) parts, 2-aminoethyl mercaptan 6 Prostitute, xylene 3 prostitute,
14 parts of a mixture of 3 parts of citrus butyl peroxide
After heating to 0° C. and reacting under reflux for 4 hours, the solvent was removed under reduced pressure to obtain 258 parts of a reaction product.
この生成物の粘度は34000センチポイズ/25℃、
硫黄含量は9.1重量%であつた。試料B
2−アミノエチルメルカプタン(1)部の代りに2ーメ
チルカプトエタノール6娼を用いた他は試料Aの場合と
まつたく同様にして反応させ、硫黄含量8.鍾量%、粘
度27500センチポイズ/25℃の反応生成物を得た
。The viscosity of this product is 34,000 centipoise/25°C;
The sulfur content was 9.1% by weight. Sample B The reaction was carried out in exactly the same manner as in Sample A, except that 6 parts of 2-methylcaptoethanol was used in place of (1) part of 2-aminoethylmercaptan, and the sulfur content was 8. A reaction product having a weight of % and a viscosity of 27,500 centipoise/25°C was obtained.
試料C
2−アミノエチルメルカプタン(1)部の代りにn−ブ
チルメルカプタン6?を用いた他は試料Aの場合とまつ
たく同様にして反応させ、硫黄含量7.鍾量%、粘度2
100センチポイズ/25℃の反応生成物を得た。Sample C 6 parts of n-butyl mercaptan instead of (1) part of 2-aminoethyl mercaptan? The reaction was carried out in the same manner as for sample A except that sulfur content was 7. Thickness %, viscosity 2
A reaction product of 100 centipoise/25°C was obtained.
試料D
2−アミノエチルメルカプタン(1)部の代りにチオグ
リコール酸旬部を用いた他は試料Aの場合とまつたく同
様にして反応させ、硫黄含量9.踵量%、粘度3100
0センチポイズ/25℃の反応生成物を得た。Sample D The reaction was carried out in exactly the same manner as in Sample A except that thioglycolic acid 1 part was used instead of 2-aminoethyl mercaptan (1 part), and the sulfur content was 9. Heel weight%, viscosity 3100
A reaction product of 0 centipoise/25°C was obtained.
試料E
試料Aの製造時において使用したポリブタジエンの代り
に市販の液状シスー1.4ポリブタジエン”(商品名
ポリオイル110、ヒユルス社製、数平均分子量160
0、シスー1.4=74%、トランスー1.4=25%
、ビニル1%)を用いる以外はすべて試料Aの場合と同
様に反応させ、硫黄含量8.鍾量%、粘度13000セ
ンチポイズ/25℃の反応生成物を得・た。Sample E Instead of the polybutadiene used in the production of Sample A, commercially available liquid 1.4 polybutadiene (trade name) was used.
Polyoil 110, manufactured by Hyuls, number average molecular weight 160
0, Sis-1.4 = 74%, Trans-1.4 = 25%
The reaction was carried out in the same manner as in Sample A except that sulfur content 8. A reaction product was obtained with a weight of 13,000 centipoise/25° C. and a viscosity of 13,000 centipoise/25°C.
試料F
試料Aの製造時において使用したポリブタジエンの代り
に市販の液状1.2−ポリブタジエン(日本曹達社製、
数平均分子量1000.ビニル90%)をj用いる以外
はすべて試F4Aの場合と同様に反応させ、硫黄含量9
.鍾量%、半固体状の反応生成物を得た。Sample F Commercially available liquid 1,2-polybutadiene (manufactured by Nippon Soda Co., Ltd.,
Number average molecular weight 1000. The reaction was carried out in the same manner as in Test F4A except that 90% vinyl) was used, and the sulfur content was 9.
.. A semi-solid reaction product was obtained.
試料G
試料Aの製造時において使用したポリブタジエンの代り
に市販の液状ポリブタジエン(日石化学社製B−200
01数平均分子量200へビニル65%、1.4一結合
35%)を用いる以外はすべて試料Aの場合と同様に反
応させ、硫黄含量8.9重量%、粘度65000センチ
ポイズ/25℃の反応生成物!を得た。Sample G Commercially available liquid polybutadiene (B-200 manufactured by Nisseki Chemical Co., Ltd.) was used instead of the polybutadiene used in the production of Sample A.
The reaction was carried out in the same manner as in Sample A except that 01 (number average molecular weight 200, 65% vinyl, 35% 1.4 bond) was used, and the reaction product had a sulfur content of 8.9% by weight and a viscosity of 65000 centipoise/25°C. thing! I got it.
試料H
ニツケルナフテネートージエチルアルミニウムクロリド
ー水を触媒としてベンゼン溶媒中で1.3−ペンタジエ
ンを重合させて得た液状ポリペンタ1ジエン(数平均分
子量32001よう素価347、シス(1.4+1.2
)=75.9%、トランス(1.4+1.2)=24.
1%)をポリブタジエンに代えて用いる以外は試料Aと
まつたく同様にして反応を行い、硫黄含量7.鍾量%、
粘度19500センチポイズ/25℃の反1応生成物を
得た。Sample H Nitchennaphthenate diethylaluminum chloride Liquid polypentadiene obtained by polymerizing 1.3-pentadiene in a benzene solvent using water as a catalyst (number average molecular weight 32001 iodine value 347, cis (1.4+1.2
)=75.9%, transformer (1.4+1.2)=24.
The reaction was carried out in exactly the same manner as in sample A except that polybutadiene (1%) was used instead of polybutadiene, and the sulfur content was 7. Limeage %,
A reaction product having a viscosity of 19,500 centipoise/25°C was obtained.
試料1
試料Aの製造時において使用したポリブタジエンの代り
に生亜麻仁油を用いる以外はすべて試料Aの場合と同様
に反応させたところ、硫黄含量20.5重量%の附加物
しか得られなかつた。Sample 1 When the reaction was carried out in the same manner as in Sample A except that raw linseed oil was used in place of the polybutadiene used in the production of Sample A, only an additive with a sulfur content of 20.5% by weight was obtained.
実施例1(1)水溶性ワニスの調製
参考例で得られた各試料1(1)部に対して20部*の
ブチルセロソルブを添加し、含有硫黄量の0.9当量に
相当する乳酸及び同当量のブチルグリシジルエーテルと
蒸留水3娼を加えて60℃にて2時間攪拌したのち、蒸
留水をさらに加えて固形分濃度40%、PH3〜7の水
溶性ワニスを調製した。Example 1 (1) Preparation of water-soluble varnish 20 parts* of butyl cellosolve was added to 1 (1) part of each sample obtained in the reference example, and lactic acid and cellosolve corresponding to 0.9 equivalents of the sulfur content were added. After adding an equivalent amount of butyl glycidyl ether and 3 parts of distilled water and stirring at 60°C for 2 hours, distilled water was further added to prepare a water-soluble varnish with a solid content concentration of 40% and a pH of 3 to 7.
))顔料分散物の調製
(1)で調製した水溶性ワニス100部、酸化チタン2
5部、オレイン酸鉛1部、カーボンブラック0.3部を
混合し、顔料分散機にて1時間攪拌してペースト状の分
散物を得た。)) Preparation of pigment dispersion 100 parts of the water-soluble varnish prepared in (1), 2 parts of titanium oxide
5 parts of lead oleate, 1 part of lead oleate, and 0.3 parts of carbon black were mixed and stirred for 1 hour using a pigment disperser to obtain a paste-like dispersion.
()水溶液の調製
(2)で調製した分散物126部、(1)で得られた水
溶性ワニス1印部を混合し、蒸留水を加えて固形分10
%、PH3〜7の水溶液を調製した。() Preparation of aqueous solution 126 parts of the dispersion prepared in (2) and 1 part of the water-soluble varnish obtained in (1) were mixed, and distilled water was added to make the solid content 10.
%, pH 3 to 7 was prepared.
1)電着条件
(3)で調製した水溶液を電着液として、燐酸鉄処理の
ダル鋼板を陰極として浴温度25℃、極間距離7crr
i(i)条件下で5.0〜120Vの電圧下て2分間通
電し、通電終了後に陰極で電着塗装された試験片をとり
出して水洗し、風乾したのち所定の温度で3紛間焼付け
た。1) Electrodeposition conditions: Using the aqueous solution prepared in (3) as the electrodeposition liquid, using the iron phosphate-treated dull steel plate as the cathode, the bath temperature was 25°C, and the distance between the electrodes was 7 crr.
Under i (i) conditions, electricity was applied for 2 minutes under a voltage of 5.0 to 120V, and after the electricity was finished, the test piece coated with cathode electrodeposition was taken out, washed with water, air-dried, and then powdered at a specified temperature for 3 minutes. Burnt.
得られた焼付け皮膜の性能を測定し、第1表に示す結果
を得た。耐食性、耐衝撃性、塗膜外観などの面において
非常にすぐれていることがわかる。一方、ビニル含量が
90%のポリブタジエンはメルカプタン化合物の附加反
応の段階でほとんどゲル状となり、これを水溶化するの
がきわめて難しく、したがつて平滑なフィルムが得られ
ない(組成物F)。またビニル含量が65%のポリブタ
ジエンでは平滑なフィルムは得られるが、流動性に乏し
いために光沢がなく、耐食性にも劣つている。一方、ポ
リペンタジエンを出発物質とした場合には塗膜が全般に
もろく、耐食性や耐水性にも劣つている(組成物H)。
さらに天然乾性油からは充分な塗膜を得ることができな
い(組成物1)。比較例1
2−アミノエチルメルカプタン2(代)部、ジーターシ
ヤリイブチルバーオキシド5部を使用すること以外は、
参考例における試料Aの調製条件に準じてメルカプタン
附加反応を行い、硫黄含有量26%の生成物を得た。The performance of the obtained baked film was measured, and the results shown in Table 1 were obtained. It can be seen that it has excellent corrosion resistance, impact resistance, and coating appearance. On the other hand, polybutadiene with a vinyl content of 90% becomes almost gel-like at the stage of the addition reaction with the mercaptan compound, and it is extremely difficult to make it water-soluble, so that a smooth film cannot be obtained (composition F). In addition, polybutadiene with a vinyl content of 65% provides a smooth film, but lacks luster due to poor fluidity and is also poor in corrosion resistance. On the other hand, when polypentadiene is used as a starting material, the coating film is generally brittle and has poor corrosion resistance and water resistance (composition H).
Furthermore, it is not possible to obtain sufficient coatings from natural drying oils (composition 1). Comparative Example 1 Except for using 2 parts of 2-aminoethyl mercaptan and 5 parts of tertiary butyl peroxide,
Mercaptan addition reaction was carried out according to the preparation conditions of Sample A in Reference Example to obtain a product with a sulfur content of 26%.
これを用いて実施例1に準じて陰極析出電着塗装を行い
、190℃で30分焼付けたところ、塗膜硬度はωであ
り、また耐塩水噴霧試験においては15時間で全面に点
錆を発生した比較例2
参考例における試料Aの調製において数平均分子量60
00の液状ポリブタジエンを用いること以外はすべて試
料Aの場合と同様に行つたところ、メルカプタン化合物
との反応生成物が一部ゲル化を起こし、これを水溶化し
て電着塗装しても平滑な塗膜が得られなかつた。Using this, cathodic electrodeposition coating was performed according to Example 1, and when baked at 190°C for 30 minutes, the coating film hardness was ω, and the salt spray resistance test showed spot rust on the entire surface after 15 hours. Comparative Example 2 In the preparation of Sample A in the Reference Example, the number average molecular weight was 60.
When all the procedures were carried out in the same manner as in the case of Sample A except that liquid polybutadiene No. 00 was used, the reaction product with the mercaptan compound partially gelled, and even if it was water-solubilized and electrodeposited, a smooth coating could not be obtained. No film was obtained.
Claims (1)
均分子量500〜5000の液状ポリブタジエンとメル
カプタン化合物とを反応して得られるスルフィド結合を
有し、かつ硫黄含有量1.5〜25重量%のメルカプタ
ン変性ポリブタジエンを少なくとも部分的にスルホニウ
ムイオン化して得られる水溶性または水分散性樹脂を含
有することを特徴とする水性被覆用組成物。 2 ポリブタジエンが1.4−結合を50%以上含有す
るものである特許請求の範囲第1項記載の組成物。 3 メルカプタン化合物が炭素数12以下のメルカプト
基含有化合物である特許請求の範囲第1項記載の組成物
。[Scope of Claims] 1. A polybutadiene having a sulfide bond obtained by reacting a mercaptan compound with a liquid polybutadiene having a number average molecular weight of 500 to 5,000 and having at least 40% of 1.4-bonds, and having a sulfur content of 1. An aqueous coating composition comprising a water-soluble or water-dispersible resin obtained by at least partially sulfonium ionizing 5 to 25% by weight of mercaptan-modified polybutadiene. 2. The composition according to claim 1, wherein the polybutadiene contains 50% or more of 1,4-bonds. 3. The composition according to claim 1, wherein the mercaptan compound is a mercapto group-containing compound having 12 or less carbon atoms.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3081078A JPS6054352B2 (en) | 1978-03-17 | 1978-03-17 | Aqueous coating composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3081078A JPS6054352B2 (en) | 1978-03-17 | 1978-03-17 | Aqueous coating composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54123144A JPS54123144A (en) | 1979-09-25 |
| JPS6054352B2 true JPS6054352B2 (en) | 1985-11-29 |
Family
ID=12314038
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3081078A Expired JPS6054352B2 (en) | 1978-03-17 | 1978-03-17 | Aqueous coating composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6054352B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP7758916B2 (en) * | 2021-04-30 | 2025-10-23 | 横浜ゴム株式会社 | Modified liquid diene polymer and method for producing the same |
| EP4729575A1 (en) * | 2023-06-16 | 2026-04-22 | Kuraray Co., Ltd. | Rubber composition and tire rubber composition |
| WO2024257655A1 (en) * | 2023-06-16 | 2024-12-19 | 株式会社クラレ | Modified liquid diene polymer and additive for rubber |
-
1978
- 1978-03-17 JP JP3081078A patent/JPS6054352B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54123144A (en) | 1979-09-25 |
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