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JPH027338B2 - - Google Patents
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JPH027338B2 - - Google Patents

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Publication number
JPH027338B2
JPH027338B2 JP8007782A JP8007782A JPH027338B2 JP H027338 B2 JPH027338 B2 JP H027338B2 JP 8007782 A JP8007782 A JP 8007782A JP 8007782 A JP8007782 A JP 8007782A JP H027338 B2 JPH027338 B2 JP H027338B2
Authority
JP
Japan
Prior art keywords
weight
carbon
acid
added
compound
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
JP8007782A
Other languages
Japanese (ja)
Other versions
JPS58198577A (en
Inventor
Yutaka Ootsuki
Yoshihiko Araki
Hiroyoshi Oomika
Hajime Hara
Kazuho Aoyama
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.)
Eneos Corp
Original Assignee
Nippon Oil Corp
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 Nippon Oil Corp filed Critical Nippon Oil Corp
Priority to JP8007782A priority Critical patent/JPS58198577A/en
Priority to US06/493,277 priority patent/US4563501A/en
Priority to EP83302677A priority patent/EP0094788B1/en
Priority to DE8383302677T priority patent/DE3366010D1/en
Publication of JPS58198577A publication Critical patent/JPS58198577A/en
Publication of JPH027338B2 publication Critical patent/JPH027338B2/ja
Granted legal-status Critical Current

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Description

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

本発明は、低温硬化性の優れた陰極析出型電着
塗料組成物に関する。 或る種の塩基性基を有する樹脂は、水中で陽イ
オン樹脂を生じ、これを用いて電着塗装を行うと
きは、樹脂が陰極に析出する。この種の、陰極析
出型塗料は、酸基を有する樹脂を塩基で中和し、
水溶性とした従来の、陽極析出型電着塗料の、本
質的な欠点、即ち、塗料浴への被塗物金属の溶出
およびそれに起因する各種の問題点を解消するこ
とができる。 本発明者等は、かかる陰極析出型塗料について
研究し、前に炭素―炭素二重結合を有する低重合
度合成重合体例えば液状ポリブタジエンのような
不飽和基含有高分子量化合物にアミノ基を導入し
酸で中和することにより優れた被膜特性を与える
陰極析出型電着塗料用樹脂が得られることを見出
し特許を出願した(特開昭51−119727、特開昭52
−147638、特開昭53−16048)。 上記の樹脂を塗膜成分とする陰極析出型電着塗
料組成物は、主として樹脂が含有する不飽基の酸
化重合により硬化し、性能の優れた塗膜を与える
が、実用的な硬化時間で硬化させるためには比較
的高い焼付温度を必要とする。本発明者らは焼付
温度を下げる研究をした結果、水溶性マンガン塩
などの金属ドライヤーを添加することにより比較
的低い焼付温度で塗膜を硬化させることを見い出
し特許を出願した(特開昭53−142444)。この場
合多量のドライヤーを必要とし、つきまわり性な
どの電着塗装性能を悪化させたり、塗面が荒れや
すいなどの問題を生じる。又本発明者らは反応性
の高いアクリル(メタクリル)性二重結合を樹脂
に導入し比較的低い焼付温度で硬化させる方法も
見出し特許を出願した(特開昭56−151777)。こ
の場合水溶性マンガン塩を添加すると160℃とい
う比較的低い温度で硬化し優れた性能を有する陰
極析出型電着塗料が得られる。しかし近年省エネ
ルギーの観点から更に焼付温度を下げることが望
まれており、本発明者らは種々研究した結果、炭
素―炭素二重結合とアミノ基を有する樹脂に炭素
−炭素二重結合とスルホン酸基あるいはコハク酸
基を有する高分子化合物の油溶性マンガン塩を添
加すると更に焼付温度を下げることができること
を見い出し本発明に到達した。 従つて本発明の目的は上記炭素―炭素二重結合
およびアミノ基含有高分子化合物の硬化性を改良
して低温硬化性と優れた耐食性を有する陰極析出
型電着塗料を提供することにある。 本発明の(A)成分の出発原料である500〜10000の
分子量で50〜500のヨウ素価の炭素―炭素二重結
合を有する高分子化合物は従来公知の方法で製造
される。 すなわちアルカリ金属または有機アルカリ金属
化合物を触媒として炭素数4〜10の共役ジオレフ
イン単独、あるいはこれらのジオレフイン同志、
あるいは共役ジオレフインに対して50モル%以下
の量の芳香族ビニルモノマー、例えばスチレン、
α―メチルスチレン、ビニルトルエン又はジビニ
ルベンゼン、とを0℃〜100℃の温度でアニオン
重合または共重合させる方法が代表的な製造方法
である。この場合分子量を制御し、ゲル分などの
少ない、淡色の低重合体を得るためにはベンジル
ナトリウムのような有機アルカリ金属化合物を触
媒とし、アルキルアリール基を有する化合物例え
ばトルエンを連鎖移動剤とする連鎖移動重合法
(米国特許第3789090号)あるいはテトラヒドロフ
ラン溶媒中でナフタリンのような多環芳香族化合
物を活性剤とし、ナトリウムのようなアルカリ金
属を触媒とするリビング重合法(特公昭42―
17485号、同43―27432号)あるいはトルエン、キ
シレンのような芳香族炭化水素を溶媒とし、ナト
リウムのようなアルカリ金属の分散体を触媒と
し、ジオキサンのようなエーテル類を添加して分
子量を制御する重合法(特公昭32−7446号、同38
―1245号、同34―10188号)などが好適な製造方
法である。また8族金属例えばコバルト又はニツ
ケルのアセチルアセトナート化合物およびアルキ
ルアルミニウムハロゲニドを触媒とする配位アニ
オン重合によつて製造される(特公昭45−507号、
同46―80300号)低重合体も用いることができる。 本発明の(A)成分すなわち500〜10000の分子量で
50〜500のヨウ素価の炭素―炭素二重結合および
100g当り30〜300ミリモルのアミノ基を有する高
分子化合物は従来公知の方法で製造される。 たとえば炭素―炭素二重結合を有する高分子化
合物に無水マレイン酸を付加させた後に一般式 (ここでR1は炭素数1〜20の炭化水素基、R2
およびR3は水素原子またはその一部がヒドロキ
シル基で置換されていても良い炭素数1〜20の炭
化水素基を表わす。) で示されるジアミン化合物を反応させてアミノ基
を導入する方法(特開昭51−119727、特開昭52−
147638、特開昭53−8629、特開昭53−63439)あ
るいは炭素―炭素二重結合を有する高分子化合物
をエポキシ化した後一級又は二級アミンを付加さ
せる方法(特開昭53−16048、特開昭53−117030)
などが知られている。 本発明の(B)成分すなわち一般式 〔式中R5及びR6は水素原子または炭素数1〜
10のアルキル基、nは0ないし20の整数、mは1
または0、Yは炭素数3か4のα,β不飽和モノ
カルボン酸の残基、そしてY′はmが0のときは
水素原子であり、mが1のときはYを表わす〕 で表わされる化合物または下記一般式(b′) 〔式中n′は0ないし10の整数、R7は水素原子ま
たは炭素数1〜10の炭化水素基、そしてYは炭素
数3か4のα,β不飽和モノカルボン酸の残基を
表わす〕 化合物を添加すると耐食性が著しく改善される。 成分(B)の含有量は、樹脂(A)の100重量部に対し、
3〜100重量部、好ましくは10〜50重量部の範囲
である。 成分(B)の含有量がこれより少ないと、耐食性の
改善が充分でなく、これより多いと、水分散性を
悪化させる。 上記成分(B)の化合物を得るには、 式 〔R5,R6は水素原子又は炭素原子数1〜10の
アルキル基好ましくはメチル基、エチル基、nは
0ないし20好ましくは1ないし5の整数、mは0
又は1、好ましくは1である〕 で示されるグリシジル化合物を原料に用いる。こ
のグリシジル化合物は通常アルカリの存在下でビ
スフエノールをエピクロルヒドリンでエーテル化
することによつて作ることができる。このような
ビスフエノール化合物としては2,2―ビス
(4′―ヒドロキシフエニル)プロパン、1,1―
ビス(4′―ヒドロキシフエニル)エタン、1,1
―ビス(4′―ヒドロキシフエニル)イソブタン、
などである。多くの場合上記のグリシジルエーテ
ルをビスフエノールなどと更に反応させ、次いで
この生成物をエピクロルヒドリンと更に反応させ
ると幾分高い分子量を有するグリシジル化合物が
合成され、これらを使用することができる。 次に上記グリシジル化合物を温度0〜200℃好
ましくは50〜150℃で炭素数3か4の不飽和カル
ボン酸と反応させる。炭素数3か4の不飽和カル
ボン酸とは、アクリル酸、メタクリル酸およびク
ロトン酸等であり、それらの混合物も使用でき
る。 反応には第3級アミン類や第4アンモニウム塩
類などの適当な触媒を用いることができる。また
溶媒の存在下、非存在下で反応を行なうことがで
きるが、溶媒を使用する場合は、樹脂(A)の合成に
際して、一級または二級アミンを反応させる段階
で使用する溶媒と同種のものを使用することがで
きる。 上記の反応は、不飽和カルボン酸として、例え
ばアクリル酸を用いる場合には下記反応式 に従つて進行する。 本発明においては、上記のグリシジル化合物分
子中の
The present invention relates to a cathodically deposited electrodeposition coating composition having excellent low-temperature curability. A resin having a certain type of basic group forms a cationic resin in water, and when this is used for electrodeposition coating, the resin is deposited on the cathode. This type of cathodically deposited paint neutralizes a resin with acid groups with a base,
It is possible to eliminate the essential drawbacks of conventional water-soluble anodic electrodeposition paints, that is, elution of the metal to be coated into the paint bath and various problems caused by this. The present inventors have conducted research on such cathodic deposition coatings, and have previously introduced amino groups into unsaturated group-containing high molecular weight compounds such as low polymerization degree synthetic polymers having carbon-carbon double bonds, such as liquid polybutadiene. He discovered that a resin for cathodically deposited electrodeposition paints that gave excellent coating properties could be obtained by neutralizing it with an acid, and applied for a patent (JP-A-51-119727, JP-A-52
−147638, Japanese Patent Publication No. 53-16048). Cathode-deposited electrodeposition coating compositions containing the above-mentioned resins as coating film components are cured mainly through oxidative polymerization of unsaturated groups contained in the resins, and provide coatings with excellent performance. Requires relatively high baking temperatures for hardening. As a result of research on lowering the baking temperature, the present inventors discovered that by adding a metal dryer such as a water-soluble manganese salt, the coating film could be cured at a relatively low baking temperature, and filed a patent application (Japanese Patent Laid-Open No. 53 −142444). In this case, a large amount of dryer is required, which causes problems such as deterioration of electrodeposition coating performance such as throwing power and the tendency for the coated surface to become rough. The present inventors also proposed a method for introducing highly reactive acrylic (methacrylic) double bonds into a resin and curing the resin at a relatively low baking temperature, and filed a patent application (Japanese Patent Application Laid-Open No. 151777-1982). In this case, when a water-soluble manganese salt is added, a cathodically deposited electrodeposition paint that cures at a relatively low temperature of 160° C. and has excellent performance can be obtained. However, in recent years, there has been a desire to further lower the baking temperature from the perspective of energy conservation, and as a result of various studies, the present inventors found that carbon-carbon double bonds and sulfonic acid The present inventors have discovered that the baking temperature can be further lowered by adding an oil-soluble manganese salt of a polymer compound having a succinic acid group or a succinic acid group. Therefore, an object of the present invention is to improve the curability of the above-mentioned carbon-carbon double bond and amino group-containing polymer compound to provide a cathodically deposited electrodeposition paint having low temperature curability and excellent corrosion resistance. The starting material for component (A) of the present invention, a polymer compound having a carbon-carbon double bond with a molecular weight of 500 to 10,000 and an iodine value of 50 to 500, is produced by a conventionally known method. That is, a conjugated diolefin having 4 to 10 carbon atoms alone or a combination of these diolefins using an alkali metal or an organic alkali metal compound as a catalyst,
or an aromatic vinyl monomer, such as styrene, in an amount of 50 mol% or less based on the conjugated diolefin;
A typical manufacturing method is anionic polymerization or copolymerization of α-methylstyrene, vinyltoluene, or divinylbenzene at a temperature of 0°C to 100°C. In this case, in order to control the molecular weight and obtain a light-colored low polymer with little gel content, an organic alkali metal compound such as sodium benzyl is used as a catalyst, and a compound having an alkylaryl group, such as toluene, is used as a chain transfer agent. Chain transfer polymerization method (U.S. Patent No. 3789090) or living polymerization method (Japanese Patent Publication No. 1973-1983) using a polycyclic aromatic compound such as naphthalene as an activator and an alkali metal such as sodium as a catalyst in a tetrahydrofuran solvent.
17485, 43-27432) or aromatic hydrocarbons such as toluene or xylene as a solvent, a dispersion of an alkali metal such as sodium as a catalyst, and an ether such as dioxane added to control the molecular weight. Polymerization method (Special Publication No. 32-7446, No. 38)
-1245, No. 34-10188) are suitable manufacturing methods. It is also produced by coordination anionic polymerization using an acetylacetonate compound of a Group 8 metal such as cobalt or nickel and an alkyl aluminum halide (Japanese Patent Publication No. 45-507,
(No. 46-80300) Low polymers can also be used. Component (A) of the present invention, that is, a molecular weight of 500 to 10,000
Carbon-carbon double bonds with an iodine value of 50 to 500 and
A polymer compound having 30 to 300 mmol of amino groups per 100 g is produced by a conventionally known method. For example, after adding maleic anhydride to a polymer compound with carbon-carbon double bonds, the general formula (Here, R 1 is a hydrocarbon group having 1 to 20 carbon atoms, R 2
and R 3 represents a hydrocarbon group having 1 to 20 carbon atoms, in which a hydrogen atom or a portion thereof may be substituted with a hydroxyl group. ) A method of introducing an amino group by reacting a diamine compound represented by
147638, JP-A-53-8629, JP-A-53-63439) or a method of adding a primary or secondary amine after epoxidizing a polymer compound having a carbon-carbon double bond (JP-A-53-16048, JP-A-53-117030)
etc. are known. Component (B) of the present invention, that is, general formula [In the formula, R 5 and R 6 are a hydrogen atom or a carbon number of 1 to
10 alkyl groups, n is an integer from 0 to 20, m is 1
or 0, Y is the residue of an α,β unsaturated monocarboxylic acid having 3 or 4 carbon atoms, and Y′ is a hydrogen atom when m is 0, and Y when m is 1] or the following general formula (b′) [In the formula, n' is an integer from 0 to 10, R 7 is a hydrogen atom or a hydrocarbon group having 1 to 10 carbon atoms, and Y represents a residue of an α,β unsaturated monocarboxylic acid having 3 or 4 carbon atoms. ] Corrosion resistance is significantly improved by adding the compound. The content of component (B) is 100 parts by weight of resin (A),
It ranges from 3 to 100 parts by weight, preferably from 10 to 50 parts by weight. If the content of component (B) is less than this, corrosion resistance will not be improved sufficiently, and if it is more than this, water dispersibility will deteriorate. To obtain the compound of component (B) above, use the formula [R 5 and R 6 are a hydrogen atom or an alkyl group having 1 to 10 carbon atoms, preferably a methyl group or an ethyl group, n is an integer of 0 to 20, preferably 1 to 5, and m is 0
or 1, preferably 1] is used as a raw material. This glycidyl compound can be prepared by etherifying bisphenol with epichlorohydrin, usually in the presence of an alkali. Such bisphenol compounds include 2,2-bis(4'-hydroxyphenyl)propane, 1,1-
Bis(4'-hydroxyphenyl)ethane, 1,1
-bis(4′-hydroxyphenyl)isobutane,
etc. In many cases, further reaction of the above glycidyl ethers with bisphenols and the like, and then further reaction of this product with epichlorohydrin, synthesizes glycidyl compounds with somewhat higher molecular weights, which can be used. Next, the glycidyl compound is reacted with an unsaturated carboxylic acid having 3 or 4 carbon atoms at a temperature of 0 to 200°C, preferably 50 to 150°C. Unsaturated carboxylic acids having 3 or 4 carbon atoms include acrylic acid, methacrylic acid, crotonic acid, etc., and mixtures thereof can also be used. Appropriate catalysts such as tertiary amines and quaternary ammonium salts can be used for the reaction. The reaction can be carried out in the presence or absence of a solvent, but if a solvent is used, it should be the same type as the solvent used in the step of reacting the primary or secondary amine during the synthesis of the resin (A). can be used. In the above reaction, when using acrylic acid as the unsaturated carboxylic acid, for example, the reaction formula is as follows: Proceed according to. In the present invention, in the above glycidyl compound molecule,

【式】基が残存しないように その実質的に全てが該不飽和カルボン酸と反応し
[Formula] Substantially all of the group is reacted with the unsaturated carboxylic acid so that no group remains.

【式】基(Yは前記と同じ意 味を有する)に変換されることが要求される。[Formula] Group (Y has the same meaning as above) taste).

【式】基が残存するならば、この基 は、後に酸を加えて水溶化する際に樹脂(A)の有す
る塩基性基と不都合な反応をし、ゲル化を起こす
結果、粘度が高くなりすぎて水溶化ができない。
たとえば水溶化ができた場合でも水溶液が経時変
化を起こし、一定の電着特性、あるいは電着塗膜
が得られないなどの欠点を生じる。 従来、ビスフエノール型のエポキシ樹脂は、耐
食性にすぐれた樹脂として知られており、これに
架橋性をもたせるためにエポキシ基の一部を残し
たり、(特公昭49−23807、特公昭51−15860)、ブ
ロツクイソシアネート化合物を架橋剤に用いるな
どの試みがなされている。しかしながら、このよ
うな塗料は実用的な硬度を得るためには200℃以
上のごとき高温が要求され、比較的低温で硬化で
きる場合にも狭い範囲の焼付温度しか選択できな
いなどの欠点があつた。 さらにビスフエノール型エポキシ樹脂は実用的
な電着条件下では或程度の高分子量体を有するも
の用いなければならず、必然的に塗膜が柔軟性に
欠けるきらいがある。また炭素―炭素二重結合を
有する樹脂にブロツクイソシアネートを用いる場
合には焼付時の酸化重合が阻害されて十分な性能
を有する塗膜が得られない傾向がある。 従つて、本発明により、前記グリシジル化合物
[Formula] If the group remains, this group will react unfavorably with the basic group of the resin (A) when an acid is added later to make it water-solubilized, resulting in gelation and increased viscosity. So it cannot be water-solubilized.
For example, even if water-solubilization is achieved, the aqueous solution changes over time, resulting in disadvantages such as unsteady electrodeposition characteristics or an inability to obtain an electrodeposited coating. Traditionally, bisphenol-type epoxy resins have been known as resins with excellent corrosion resistance. ), attempts have been made to use blocked isocyanate compounds as crosslinking agents. However, such paints require high temperatures of 200°C or higher to obtain practical hardness, and even when they can be cured at relatively low temperatures, they have the disadvantage that only a narrow range of baking temperatures can be selected. Furthermore, the bisphenol type epoxy resin must have a certain degree of high molecular weight under practical electrodeposition conditions, and the coating film inevitably tends to lack flexibility. Furthermore, when a blocked isocyanate is used in a resin having carbon-carbon double bonds, oxidative polymerization during baking tends to be inhibited, making it difficult to obtain a coating film with sufficient performance. Therefore, according to the present invention, the glycidyl compound

【式】基の実質的に全てが、[Formula] Substantially all of the groups are

【式】に変換された化合物(B)を 陰極析出型電着塗料の一成分として、前記樹脂、
(A)と併用することができ、それによつて、樹脂(A)
の、優れた硬化性と被膜特性を何等損うことな
く、その耐食性を顕著に改善できることが見出さ
れたことは、真に驚くべきである。 成分(C)の300〜3000の分子量で50〜500のヨウ素
価の炭素―炭素二重結合および100g当り30〜300
ミリモルのスルホン酸基あるいはコハク酸基を有
する高分子化合物の油溶性マンガン塩を0.2〜20
重量部添加することにより著しく硬化性が促進さ
れ低温硬化性の陰極析出型電着塗料が得られる。 一般に油溶性のマンガン塩としてはナフテン酸
マンガン、オクテン酸マンガン、マンガンアセチ
ルアセトナートなどが知られているが、これらの
マンガン塩は弱酸のマンガン塩であり、中和剤の
酢酸などと水溶液で交換反応を生じ徐々に水塩性
のマンガン塩になり、電着塗料の安定性を悪くす
る。 また水溶性のマンガン塩が生成すると水溶性の
マンガン塩は電着塗料液の電導度を上昇させるた
め肌荒れの原因になるあるいは水溶性のマンガン
塩は油溶性のマンガン塩に比べて硬化を促進する
効果が小さいので硬化性が低下するなどの問題点
があり、油溶性でも弱酸のマンガン塩の使用は好
ましくない。また上記弱酸のマンガン塩は実質的
には不飽和基を有していないので成分(A)あるいは
成分(B)の樹脂と共硬化しないため、耐溶剤性など
焼付塗膜の性能を低下させる原因にもなる。 本発明で用いられる油溶性スルホン酸のマンガ
ン塩あるいはコハク酸のマンガン塩は強酸の塩で
あるため中和剤の酢酸などと交換反応を生じない
し、不飽和基を有しているので成分(A)あるいは成
分(B)と焼付時に共硬化するので上記問題点を生じ
ることなく使用することができる。 本発明で用いられる(C)成分すなわち300〜3000
の分子量で50〜500のヨウ素価の炭素―炭素二重
結合および100g当り30〜30ミリモルのスルホン
酸基あるいはコハク酸基を有する高分子量化合物
の油溶性マンガン塩は従来公知の方法で製造され
る。たとえば本発明の(A)成分の出発原料に用いら
れる共役ジオレフインの低重合体あるいは共低重
合体をスルホン化あるいはマレイン化した後、こ
れらの酸基のナトリウム塩と硫酸マンガン、塩化
マンガンなどとの塩交換反応によるいわゆる複分
解法あるいはアセチルアセトマンガン、炭酸マン
ガン、酢酸マンガンなどの弱酸のマンガン塩との
酸交換反応による方法で容易に製造される。 本発明の成分(C)の油溶性マンガン塩の添加量は
0.2重量部より少ないと硬化性を促進する効果が
小さく、また20重量部より多すぎると硬化性は良
いが、水分散性、耐食性などを低下させるので好
ましくない。好ましい範囲は1〜10重量部であ
り、マンガン金属量としては0.05〜0.5重量部が
好ましい。 本発明において成分(A)、成分(B)および成分(C)か
らなる組成物を水溶化または水分散化するために
は成分(A)、成分(B)および成分(C)をあらかじめ混合
した後、成分(A)のアミノ基に対して0.1〜2.0好ま
しくは0.2〜1.0モル当量の酢酸、プロピオン酸、
乳酸などの水溶性の有機酸で中和し、水溶化する
ことが好ましい。 本発明の樹脂組成物(a)または(c)を中和し水に溶
解または分散させるにあたり、溶解または分散を
容易にし、水溶液の安定性を向上させ、樹脂の流
動性を改善し、塗膜の平滑性を改善するなどの目
的で、水溶性でありしかも各樹脂組成物を溶解し
うるエチルセロソルブ、プロピルセロソルブ、ブ
チルセロソルブ、エチレングリコールジメチルエ
ーテル、ジエチレングリコールジメチルエーテ
ル、ジアセトンアルコール、4―メトキシ―4―
メチルペンタノン―2、メチルエチルケトンなど
の有機溶剤を各樹脂組成物100重量部当り10〜100
重量部使用することが好ましい。 本発明の陰極析出型電着塗料組成物にはさらに
適当な顔料を配合することができる。例えば酸化
鉄、酸化鉛、ストロンチウムクロメート、カーボ
ンブラツク、二酸化チタン、タルク、珪酸アルミ
ニウム、硫酸バリウムの如き顔料の一種またはそ
れ以上を配合することができる。 これらの顔料はそのまま本発明の組成物に添加
できるが、あらかじめ、成分(A)を中和し水に分散
又は水溶液化したものの一部分に多量の顔料を加
えて混合し、ペースト状のマスターバツチとした
ものを得、このペースト状の顔料を組成物に添加
することができる。 次に実施例および比較例により本発明を更に具
体的に説明する。なお実施例および比較例の塗膜
の物性テストはJIS―K―5400に準じて行なつた。 製造例 1 日石ポリブタジエンB―2000(数平均分子量
2000、1.2結合65%)を過酢酸を用いてエポキシ
化しオキシラン酸素含有量6.3%のエポキシ化ポ
リブタジエン(E1)を製造した。 このエポキシ化ポリブタジエン(E1)1076g
およびエチルセロソルブ108gを2オートクレ
ーブに仕込んだ後ジメチルアミン40gを加え、
150℃で5時間反応させた。未反応アミンを留去
した後、アクリル酸95g、ハイドロキノン8gお
よびエチルセロソルブ260gの混合物を添加し、
さらに150℃で45分反応させて本発明の成分(A)の
樹脂溶液(A1)を製造した。このもののアミン
価は50ミリモル/100g酸価は5ミリモル/100g
そして固型分濃度は75.0重量%であつた。 製造例 2 日石ポリブタジエンB―1500(数平均分子量
1500、1.2結合63%)を過酢酸を用いてエポキシ
化しオキシラン酸素含有量6.5%のエポキシ化ポ
リブタジエン(E2)を製造した。 このエポキシ化ポリブタジエン(E2)1000g
およびエチルセロソルブ368gおよびジエタノー
ルアミン105gを3セパラブルフラスコに仕込
み150℃で6時間反応させた。反応後、120℃まで
冷却し、アクリル酸79g、ハイドロキノン7.3g
およびエチルセロソルブ26gの混合物を加え、
120℃で8時間反応させて本発明の成分(A)の樹脂
溶液(A3)を製造した。 このもののアミン価は62mmol/100g、酸価
は12mmol/100g、そして固型分濃度は75重量
%であつた。 製造例 3 日石ポリブタジエンB―2000(数平均分子量
2000、1.2結合65%)1000g、無水マレイン酸168
g、キシレン10g、アンチゲン3C(住友化学商品
名)2gを還流冷却器を設置した2セパラブル
フラスコに仕込み窒素気流下にて190℃で5時間
反応させた。次に未反応無水マレイン酸、キシレ
ンを減圧下に留去し、酸価143ミリモル/100gの
マレイン化ポリブタジエン(M1)を合成した。 次にマレイン化ポリブタジエン(M1)803g、
ブチルセロソルブ156gを還流冷却器を備えた2
セパラブルフラスコに仕込み撹拌下に80℃に加
熱した。次にジメチルアミノプロピルアミン78g
を滴下し、次いでモノエタノールアミン23gを滴
下した。滴下終了後ただちに150℃に昇温し4時
間150℃で反応を続けた。減圧下に生成した水、
ブチルセロソルブおよび未反応アミンを留去し、
第三級アミン基および水酸基を有するイミド化ポ
リブタジエンを合成した。このイミド化ポリブタ
ジエンのアミン価は89ミリモル/100gであつた。
このイミド化ポリブタジエンを固形分が80重量%
になるようにエチルセロソルブに溶解し本発明の
成分(A)の樹脂溶液(A3)を製造した。 製造例 4 ビスフエノールAとエピクロルヒドリンをアル
カリ触媒の存在下で反応させて得た下記化合物 として、エポキシ当量500を持つビスフエノール
タイプエポキシ樹脂〔商品名エピコート1001シエ
ル化学(株)製〕1000gをエチルセロソルブ227gに
溶解し、アクリル酸137g、ハイドロキノン0.2g
およびN,Nジメチルアミノエタノールを5g添
加し、100℃に加熱して5時間反応させ、本発明
の成分(B)であるエポキシ樹脂―アクリル酸付加物
のエチルセロソルブ溶液(B1)を合成した。 製造例 5 エポキシ当量500を持つビスフエノールタイプ
エポキシ樹脂〔商品名エピコート1001、シエル化
学(株)製〕1000gをエチルセロソルブ288gに溶解
し、メタクリル酸164g、ハイドロキノン0.2gお
よびN,Nジメチルアミノエタノールを5g添加
し、製造例4と同様の反応条件で、本発明の成分
(B)であるエポキシ樹脂―メタクリル酸付加物のエ
チルセロソルブ溶液(B2)を合成した。 製造例 6 日石ポリブタジエンB―700(数平均分子量700、
1.2結合52%)1000g、無水マレイン酸117.3g、
アンチゲン3C1gおよびキシレン10gを還流冷却
器を設置した2セパラブルフラスコに仕込み窒
素気流下にて195℃で5時間反応させた。次に未
反応無水マレイン酸およびキシレンを減圧下に留
去し酸価107ミリモル/100gのマレイン化ポリブ
タジエン(M2)を合成した。 マレイン化ポリブタジエン(M2)500gおよび
エチルセロソルブ148gを120℃で2時間反応させ
無水コハク酸基を開環させた後室温まで冷却し、
カ性ソーダの22.5重量%水溶液100gを除々に加
え中和した後固形分濃度が25重量%になるように
脱イオン水を加えマレイン化ポリブタジエンの水
溶液を調製した。 次に硫酸マンガン(MnSO4・H2O4.5)74.5g
を水600gに溶解した後イソプロピルアルコール
600gおよびベンゼン1000gを加え撹拌下に室温
で上記マレイン化ポリブタジエンの水溶液2192g
を除々に滴下し、滴下終了後60℃に30分加熱した
後1時間静置したところ二層に分離したので下層
を切り、脱イオン水1000g加え60℃に30分加熱し
た後1時間静置し下層を除去した。 上層を取り出しベンゼンなどを減圧下で留去し
マレイン化ポリブタジエンのマンガン塩を複分解
法で製造した。 このマレイン化ポリブタジエンのマンガン塩を
固形分が75重量%になるようにエチルセロソルブ
に溶解し本発明の成分(C)の油溶性マンガン塩の溶
液(C1)を製造した。(C1)のマンガン含有量は
2重量%であつた。 製造例 7 日石ポリブタジエンB―1500 1000g、無水マ
レイン酸117.3gアンチゲン3C 2gおよびキシレ
ン10gを還流冷却器を設置した2セパラブルフ
ラスコに仕込み窒素気流下にて195℃で5時間反
応させた。次に未反応無水マレイン酸およびキシ
レンを減圧下で留去し酸価107ミリモル/100gの
マレイン化ポリブタジエン(M3)を合成した。 マレイン化ポリブタジエン(M3)250g、エチ
ルセロソルブ220gを還流冷却器およびリービツ
ヒコンデンサーを設置した1セパラブルフラス
コに仕込み120℃で2時間反応させ無水コハク酸
基を開環させた後、酢酸マンガンを46.4g溶解し
た水溶液175.7gを加え120℃に加熱し水、酢酸、
エチルセロソルブを常圧で留出させた後更に減圧
にして酢酸、エチルセロソルブを留去し酸交換法
でマレイン化ポリブタジエンのマンガン塩を製造
した。 このマレイン化ポリブタジエンのマンガン塩を
固形分が75重量%になるようにエチルセロソルブ
に溶解し本発明の成分(C)の油溶性マンガン塩の溶
液(C2)を製造した。(C2)のマンガン含有量は
3.6重量%であつた。 製造例 8 還流冷却器と滴下ロートを設置した2のセパ
ラブルフラスコに日石ポリブタジエンB−700を
100g採取し、これに脱水ジクロルエタン1200ml
を加えて溶解し5℃に冷却した。温度を5℃に保
ちながら、SO311.4gと脱水ジクロルエタン100
mlに溶解した脱水1,4ジオキサン12.6gとから
合成したSO3・ジオキサン(1:1)コンプレツ
クスを窒素気流下で60分間かけて滴下した。滴下
終了後同一温度で30分間熟成しスルホン化ポリブ
タジエン(S1)の溶液を合成した。次に2のセ
パラブルフラスコにMnCO39.1gと水18.2gを激
しく撹拌する中に熟成後の(S1)の溶液を窒素気
流下で5分間で滴下した。滴下終了後60℃に30分
間加熱し加水分解を完結させた。反応液から溶媒
を留去することによつて茶かつ色の半固体状のス
ルホン化ポリブタジエンのマンガン塩を酸交換反
応で製造した。 このスルホン化ポリブタジエンのマンガン塩を
固形分が75重量%になるようにエチルセロソルブ
に溶解し本発明の成分(C)の油溶性マンガン塩の溶
液(C3)を製造した。(C3)のマンガン含有量は
2.8重量%であつた。 実施例 1 製造例1で製造したA1400g、製造例4で製造
したB110.8.4gおよび製造例6で製造したC145g
を均一なるまで混合した後、酢酸6gを加え十分
にかきまぜ中和した。次に脱イオン水を徐々に加
え固形分濃度が20重量%の水溶液を調製した。 この20重量%水溶液2000g、カーボンブラツク
4g、塩基性硅酸鉛20gおよびガラスビーズ2000
gを5ステンレスビーカーに入れ高速回転ミキ
サーで2時間激しくかきまぜた後、ガラスビーズ
を過した後、固形分濃度が15重量%になるよう
に脱イオン水を加え、電着塗料液を調製した。 上記電着塗料液を用いてカーボン電極を陽極と
し、リン酸亜鉛処理板(日本テストパネル社、
Bt3004、0.8×70×150mm)を陰極とし陰極析出型
電着塗装を行なつた。テスト結果を表―1に示し
た。 比較例 1 製造例6で製造したC1を添加しない以外は全
て実施例1と全く同じ条件で陰極析出型電着塗料
液を調製し、実施例1と同様の条件でテストを行
ない結果を表―1に示した。 比較例 2 製造例6で製造したC1の代りに酢酸マンガン
をマンガンとして0.9g添加する以外は全て実施
例1と全く同じ条件で陰極析出型電着塗料液を調
製し、実施例1と同様の条件でテストを行ない結
果を表―1に示した。
The compound (B) converted into [Formula] is used as a component of the cathodic deposition type electrodeposition paint, and the resin,
(A), whereby the resin (A)
It is truly surprising that it has been found that it is possible to significantly improve the corrosion resistance of . Carbon-carbon double bonds of component (C) with a molecular weight of 300 to 3000 and an iodine number of 50 to 500 and 30 to 300 per 100 g
0.2 to 20 millimoles of oil-soluble manganese salt of a polymer compound having sulfonic acid groups or succinic acid groups.
By adding part by weight, curing properties are significantly accelerated, and a low-temperature curable cathodically deposited electrodeposition coating material can be obtained. In general, manganese naphthenate, manganese octenoate, manganese acetylacetonate, etc. are known as oil-soluble manganese salts, but these manganese salts are weak acid manganese salts and can be exchanged with acetic acid as a neutralizing agent in an aqueous solution. A reaction occurs and gradually turns into aqueous manganese salts, which impairs the stability of electrodeposition paints. In addition, when water-soluble manganese salts are formed, water-soluble manganese salts increase the conductivity of the electrodeposition coating solution, causing rough skin, or water-soluble manganese salts accelerate curing compared to oil-soluble manganese salts. The use of manganese salts, which are weak acids, is not preferred even if they are oil-soluble, since their effectiveness is small and there are problems such as decreased curing properties. In addition, since the manganese salt of the weak acid mentioned above does not substantially have unsaturated groups, it does not co-cure with the resin of component (A) or component (B), which causes a decrease in the performance of the baked coating film such as solvent resistance. It also becomes. Since the manganese salt of oil-soluble sulfonic acid or the manganese salt of succinic acid used in the present invention is a salt of a strong acid, it does not cause an exchange reaction with the neutralizing agent such as acetic acid, and since it has an unsaturated group, the component (A ) or co-cures with component (B) during baking, so it can be used without causing the above problems. (C) component used in the present invention, i.e. 300 to 3000
An oil-soluble manganese salt of a high molecular weight compound having a carbon-carbon double bond with a molecular weight of 50 to 500 and an iodine number of 30 to 30 mmol per 100 g of sulfonic acid or succinic acid groups is produced by a conventionally known method. . For example, after sulfonating or maleating the conjugated diolefin low polymer or co-low polymer used as the starting material for component (A) of the present invention, the sodium salt of these acid groups is combined with manganese sulfate, manganese chloride, etc. It is easily produced by a so-called double decomposition method using a salt exchange reaction or an acid exchange reaction with a manganese salt of a weak acid such as acetylacetomanganese, manganese carbonate, or manganese acetate. The amount of oil-soluble manganese salt added as component (C) of the present invention is
If it is less than 0.2 parts by weight, the effect of promoting curability is small, and if it is more than 20 parts by weight, curability is good, but water dispersibility, corrosion resistance, etc. are deteriorated, which is not preferable. The preferred range is 1 to 10 parts by weight, and the preferred amount of manganese metal is 0.05 to 0.5 parts by weight. In the present invention, in order to water-solubilize or water-disperse a composition consisting of component (A), component (B), and component (C), component (A), component (B), and component (C) are mixed in advance. After that, 0.1 to 2.0, preferably 0.2 to 1.0 molar equivalents of acetic acid, propionic acid,
It is preferable to neutralize with a water-soluble organic acid such as lactic acid to make it water-soluble. When neutralizing the resin composition (a) or (c) of the present invention and dissolving or dispersing it in water, it facilitates dissolution or dispersion, improves the stability of the aqueous solution, improves the fluidity of the resin, and improves the coating film. Ethyl cellosolve, propyl cellosolve, butyl cellosolve, ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, diacetone alcohol, 4-methoxy-4-, which are water-soluble and can dissolve each resin composition, are used for purposes such as improving the smoothness of the resin composition.
Organic solvents such as methylpentanone-2 and methyl ethyl ketone are added in an amount of 10 to 100 parts per 100 parts by weight of each resin composition.
Preferably, parts by weight are used. A suitable pigment can be further blended into the cathodically deposited electrodeposition coating composition of the present invention. For example, one or more pigments such as iron oxide, lead oxide, strontium chromate, carbon black, titanium dioxide, talc, aluminum silicate, and barium sulfate can be blended. These pigments can be added to the composition of the present invention as they are, but a large amount of pigments may be added to a portion of component (A) that has been neutralized and dispersed in water or made into an aqueous solution and mixed to form a paste-like masterbatch. This pasty pigment can be added to the composition. Next, the present invention will be explained in more detail with reference to Examples and Comparative Examples. The physical properties of the coating films of Examples and Comparative Examples were tested in accordance with JIS-K-5400. Production example 1 Nisseki polybutadiene B-2000 (number average molecular weight
2000, 1.2 bond 65%) was epoxidized using peracetic acid to produce epoxidized polybutadiene (E 1 ) with an oxirane oxygen content of 6.3%. 1076g of this epoxidized polybutadiene (E 1 )
After charging 108g of ethyl cellosolve into two autoclaves, add 40g of dimethylamine,
The reaction was carried out at 150°C for 5 hours. After distilling off the unreacted amine, a mixture of 95 g of acrylic acid, 8 g of hydroquinone and 260 g of ethyl cellosolve was added,
Further, the reaction was carried out at 150° C. for 45 minutes to produce a resin solution (A 1 ) of component (A) of the present invention. The amine value of this product is 50 mmol/100g, and the acid value is 5 mmol/100g.
The solid content concentration was 75.0% by weight. Production example 2 Nisseki polybutadiene B-1500 (number average molecular weight
1500, 1.2 bond 63%) was epoxidized using peracetic acid to produce epoxidized polybutadiene (E 2 ) with an oxirane oxygen content of 6.5%. 1000g of this epoxidized polybutadiene (E 2 )
Then, 368 g of ethyl cellosolve and 105 g of diethanolamine were charged into 3 separable flasks and reacted at 150°C for 6 hours. After the reaction, cool to 120℃ and add 79g of acrylic acid and 7.3g of hydroquinone.
Add a mixture of and 26g of ethyl cellosolve,
A resin solution (A 3 ) of component (A) of the present invention was prepared by reacting at 120° C. for 8 hours. The amine value of this product was 62 mmol/100 g, the acid value was 12 mmol/100 g, and the solid content concentration was 75% by weight. Production example 3 Nisseki polybutadiene B-2000 (number average molecular weight
2000, 1.2 bond 65%) 1000g, maleic anhydride 168
g, xylene 10 g, and Antigen 3C (trade name) 2 g were placed in a two-separable flask equipped with a reflux condenser and reacted at 190° C. for 5 hours under a nitrogen stream. Next, unreacted maleic anhydride and xylene were distilled off under reduced pressure to synthesize maleated polybutadiene (M 1 ) having an acid value of 143 mmol/100 g. Next, 803 g of maleated polybutadiene (M 1 ),
156g of butyl cellosolve was added to the 2 tubes equipped with a reflux condenser.
The mixture was placed in a separable flask and heated to 80°C with stirring. Next, 78g of dimethylaminopropylamine
was added dropwise, and then 23 g of monoethanolamine was added dropwise. Immediately after the dropwise addition was completed, the temperature was raised to 150°C and the reaction was continued at 150°C for 4 hours. water produced under reduced pressure,
Butyl cellosolve and unreacted amine are distilled off,
Imidized polybutadiene having tertiary amine groups and hydroxyl groups was synthesized. The amine value of this imidized polybutadiene was 89 mmol/100 g.
This imidized polybutadiene has a solid content of 80% by weight.
A resin solution (A 3 ) of the component (A) of the present invention was prepared by dissolving it in ethyl cellosolve so that the following was obtained. Production Example 4 The following compound obtained by reacting bisphenol A and epichlorohydrin in the presence of an alkali catalyst As follows, 1000 g of bisphenol type epoxy resin [trade name Epicote 1001 manufactured by Ciel Chemical Co., Ltd.] having an epoxy equivalent of 500 was dissolved in 227 g of ethyl cellosolve, 137 g of acrylic acid, and 0.2 g of hydroquinone.
and 5 g of N,N dimethylaminoethanol were added, heated to 100°C and reacted for 5 hours to synthesize an ethyl cellosolve solution (B 1 ) of the epoxy resin-acrylic acid adduct, which is the component (B) of the present invention. . Production Example 5 1000 g of a bisphenol type epoxy resin having an epoxy equivalent of 500 [trade name Epicote 1001, manufactured by Ciel Chemical Co., Ltd.] was dissolved in 288 g of ethyl cellosolve, and 164 g of methacrylic acid, 0.2 g of hydroquinone and N,N dimethylaminoethanol were added. The components of the present invention were added under the same reaction conditions as Production Example 4.
An ethyl cellosolve solution (B 2 ) of the epoxy resin-methacrylic acid adduct (B) was synthesized. Production example 6 Nisseki polybutadiene B-700 (number average molecular weight 700,
1.2 bond 52%) 1000g, maleic anhydride 117.3g,
1 g of Antigen 3C and 10 g of xylene were charged into a two-separable flask equipped with a reflux condenser and reacted at 195° C. for 5 hours under a nitrogen stream. Next, unreacted maleic anhydride and xylene were distilled off under reduced pressure to synthesize maleated polybutadiene (M 2 ) having an acid value of 107 mmol/100 g. 500 g of maleated polybutadiene (M 2 ) and 148 g of ethyl cellosolve were reacted at 120°C for 2 hours to open the succinic anhydride groups, and then cooled to room temperature.
After neutralizing by gradually adding 100 g of a 22.5% by weight aqueous solution of caustic soda, deionized water was added so that the solid content concentration was 25% by weight to prepare an aqueous solution of maleated polybutadiene. Next, 74.5g of manganese sulfate (MnSO 4 H 2 O 4.5 )
After dissolving in 600g of water, add isopropyl alcohol.
600g and 1000g of benzene were added, and 2192g of the above maleated polybutadiene aqueous solution was prepared at room temperature while stirring.
was gradually added dropwise, heated to 60°C for 30 minutes after dropping, and left to stand for 1 hour. It separated into two layers, so the lower layer was cut off, 1000g of deionized water was added, heated to 60°C for 30 minutes, and left to stand for 1 hour. The lower layer was removed. The upper layer was taken out and benzene etc. were distilled off under reduced pressure to produce manganese salt of maleated polybutadiene by double decomposition method. This manganese salt of maleated polybutadiene was dissolved in ethyl cellosolve so that the solid content was 75% by weight to produce a solution (C 1 ) of an oil-soluble manganese salt as component (C) of the present invention. The manganese content of (C 1 ) was 2% by weight. Production Example 7 1000 g of Nisseki Polybutadiene B-1500, 117.3 g of maleic anhydride, 2 g of Antigen 3C, and 10 g of xylene were charged into a two-separable flask equipped with a reflux condenser and reacted at 195° C. for 5 hours under a nitrogen stream. Next, unreacted maleic anhydride and xylene were distilled off under reduced pressure to synthesize maleated polybutadiene (M 3 ) having an acid value of 107 mmol/100 g. 250 g of maleated polybutadiene (M 3 ) and 220 g of ethyl cellosolve were placed in a separable flask equipped with a reflux condenser and a Liebig condenser, and reacted at 120°C for 2 hours to open the succinic anhydride groups. Add 175.7g of an aqueous solution containing 46.4g and heat to 120°C.
After ethyl cellosolve was distilled off at normal pressure, the pressure was further reduced to remove acetic acid and ethyl cellosolve, and a manganese salt of maleated polybutadiene was produced by an acid exchange method. This manganese salt of maleated polybutadiene was dissolved in ethyl cellosolve so that the solid content was 75% by weight to produce a solution (C 2 ) of oil-soluble manganese salt as component (C) of the present invention. The manganese content of (C 2 ) is
It was 3.6% by weight. Production example 8 Nisseki polybutadiene B-700 was placed in a separable flask equipped with a reflux condenser and a dropping funnel.
Collect 100g and add 1200ml of dehydrated dichloroethane to it.
was added to dissolve and cooled to 5°C. While maintaining the temperature at 5℃, add 11.4g of SO 3 and 100g of dehydrated dichloroethane.
A SO 3 dioxane (1:1) complex synthesized from 12.6 g of dehydrated 1,4 dioxane dissolved in 1 mL of the solution was added dropwise over 60 minutes under a nitrogen stream. After the dropwise addition was completed, the mixture was aged at the same temperature for 30 minutes to synthesize a solution of sulfonated polybutadiene (S 1 ). Next, while 9.1 g of MnCO 3 and 18.2 g of water were being vigorously stirred, the aged solution of (S 1 ) was added dropwise to the second separable flask under a nitrogen stream over 5 minutes. After the dropwise addition was completed, the mixture was heated to 60°C for 30 minutes to complete hydrolysis. By distilling off the solvent from the reaction solution, a brown semisolid manganese salt of sulfonated polybutadiene was produced by acid exchange reaction. This manganese salt of sulfonated polybutadiene was dissolved in ethyl cellosolve so that the solid content was 75% by weight to produce a solution (C 3 ) of oil-soluble manganese salt as component (C) of the present invention. The manganese content of (C 3 ) is
It was 2.8% by weight. Example 1 400 g of A 1 produced in Production Example 1, 10.8.4 g of B 1 produced in Production Example 4, and 45 g of C 1 produced in Production Example 6
After mixing until homogeneous, 6 g of acetic acid was added and thoroughly stirred to neutralize. Next, deionized water was gradually added to prepare an aqueous solution with a solid content concentration of 20% by weight. 2000g of this 20% aqueous solution, 4g of carbon black, 20g of basic lead silicate and 2000 glass beads.
5 g was placed in a stainless steel beaker and stirred vigorously for 2 hours using a high-speed rotating mixer. After passing through glass beads, deionized water was added so that the solid content was 15% by weight to prepare an electrodeposition coating solution. Using the above electrodeposition paint solution, a carbon electrode was used as an anode, and a zinc phosphate treated plate (Japan Test Panel Co., Ltd.,
Bt3004, 0.8 x 70 x 150 mm) was used as the cathode for cathodic deposition electrodeposition coating. The test results are shown in Table-1. Comparative Example 1 A cathode-deposited electrodeposition coating solution was prepared under the same conditions as in Example 1, except that C 1 produced in Production Example 6 was not added, and a test was conducted under the same conditions as in Example 1. The results are shown below. -1. Comparative Example 2 A cathode-deposited electrodeposition coating solution was prepared in the same manner as in Example 1, except that 0.9 g of manganese acetate was added in place of C 1 produced in Production Example 6, under the same conditions as in Example 1. The test was conducted under the following conditions and the results are shown in Table 1.

【表】 実施例 2 製造例2で製造したA2400g、製造例5で製造
したB275gおよび製造例7で製造したC216.7gを
均一なるまで混合した後、酢酸7.4gを加え十分
にかきまぜ中和した。次に脱イオン水を徐々に加
え固形分濃度が25重量%の水溶液を調製した。こ
の25重量%水溶液1000g、カーボンブラツク2.5
g、塩基性硅酸鉛25gおよびガラスビーズ1000g
を3ステンレスビーカーに入れ高速回転ミキサ
ーで2時間激しくかきまぜた後、ガラスビーズを
過した後、固形分濃度が18%になるように脱イ
オン水を加え、電着塗料液を調製した。 上記電着塗料液を用いてカーボン電極を陽極と
し、リン酸亜鉛処理板(日本テストパネル社、
Bt3004、0.8×70×150mm)を陰極とし陰極析出型
電着塗装を行なつた。テスト結果を表―2に示し
た。 比較例 3 製造例7で製造したC2を添加しない以外は全
て実施例2と全く同じ条件で陰極析出型電着塗料
液を調製し、実施例2と同様の条件でテストを行
ない結果を表―2に示した。 比較例 4 製造例7で製造したC2の代りに酢酸マンガン
をマンガンとして0.6g添加する以外は全て実施
例2と全く同じ条件で陰極析出型電着塗料液を調
製し、実施例2と同様の条件でテストを行ない結
果を表―2に示した。
[Table] Example 2 After mixing 400 g of A 2 produced in Production Example 2, 75 g of B 2 produced in Production Example 5, and 16.7 g of C 2 produced in Production Example 7 until uniform, 7.4 g of acetic acid was added and the mixture was thoroughly mixed. Stir it to neutralize it. Next, deionized water was gradually added to prepare an aqueous solution with a solid content concentration of 25% by weight. 1000g of this 25% aqueous solution, carbon black 2.5
g, 25 g of basic lead silicate and 1000 g of glass beads
The mixture was placed in a stainless steel beaker and stirred vigorously for 2 hours using a high-speed rotating mixer. After passing through glass beads, deionized water was added to give a solid content concentration of 18% to prepare an electrodeposition coating solution. Using the above electrodeposition paint solution, a carbon electrode was used as an anode, and a zinc phosphate treated plate (Japan Test Panel Co., Ltd.,
Bt3004, 0.8 x 70 x 150 mm) was used as the cathode for cathodic deposition electrodeposition coating. The test results are shown in Table-2. Comparative Example 3 A cathode-deposited electrodeposition coating solution was prepared under the same conditions as in Example 2, except that C 2 produced in Production Example 7 was not added, and a test was conducted under the same conditions as in Example 2. The results are shown below. - Shown in 2. Comparative Example 4 A cathode-deposited electrodeposition coating solution was prepared in the same manner as in Example 2, except that 0.6 g of manganese acetate was added instead of C 2 produced in Production Example 7, under the same conditions as in Example 2. The test was conducted under the following conditions and the results are shown in Table 2.

【表】 実施例 3 製造例3で製造したA3400g、製造例4で製造
したB1108.4gおよび製造例8で製造したC330g
を均一になるまで混合した後、酢酸10gを加え十
分にかきまぜ中和した。次に脱イオン水を徐々に
加え固形分濃度が30重量%の水溶液を調製した。 この30重量%水溶液1000g、カーボンブラツク
3g、塩基性硅酸鉛20gおよびガラスビーズ1000
gを3ステンレスビーカーに入れ高速回転ミキ
サーで2時間激しくかきまぜた後、ガラスビーズ
を過した後、固形分濃度が16%になるように脱
イオン水を加え、電着塗料液を調製した。 上記電着塗料液を用いてカーボン電極を陽極と
し、リン酸亜鉛処理板(日本テストパネル、
Bt3004、0.8×70×150mm)を陰極とし陰極析出型
電着塗装を行なつた。テスト結果を表―3に示し
た。 比較例 5 製造例8で製造したC3を添加しない以外は全
て実施例2と全く同じ条件で陰極析出型電着塗料
液を調製し、実施例3と同様の条件でテストを行
ない結果を表―3に示した。 比較例 6 製造例8で製造したC3の代りに酢酸マンガン
をマンガンとして0.84g添加する以外は全て実施
例3と全く同じ条件で陰極析出型電着塗料液を調
製し、実施例3と同様の条件でテストを行ない結
果を表―3に示した。
[Table] Example 3 400 g of A 3 produced in Production Example 3, 108.4 g of B 1 produced in Production Example 4, and 30 g of C 3 produced in Production Example 8
After mixing until homogeneous, 10 g of acetic acid was added and thoroughly stirred to neutralize. Next, deionized water was gradually added to prepare an aqueous solution having a solid content concentration of 30% by weight. 1000g of this 30% aqueous solution, 3g of carbon black, 20g of basic lead silicate and 1000 glass beads.
3 g was placed in a stainless steel beaker and stirred vigorously for 2 hours using a high-speed rotating mixer. After passing through glass beads, deionized water was added to give a solid content concentration of 16% to prepare an electrodeposition coating solution. Using the above electrodeposition coating liquid, a carbon electrode was used as an anode, and a zinc phosphate treated plate (Japan Test Panel,
Bt3004, 0.8 x 70 x 150 mm) was used as the cathode for cathodic deposition electrodeposition coating. The test results are shown in Table-3. Comparative Example 5 A cathode-deposited electrodeposition coating solution was prepared under exactly the same conditions as in Example 2, except that C 3 produced in Production Example 8 was not added, and a test was conducted under the same conditions as in Example 3. The results are shown below. - Shown in 3. Comparative Example 6 A cathode-deposited electrodeposition coating solution was prepared in the same manner as in Example 3, except that 0.84 g of manganese acetate was added in place of C 3 produced in Production Example 8. The test was conducted under the following conditions and the results are shown in Table 3.

【表】【table】

Claims (1)

【特許請求の範囲】 1 (A) 500〜10000の分子量で50〜500のヨウ素
価の炭素―炭素二重結合および100g当り30〜
300ミリモルのアミノ基を有する高分子化合物
100重量部 (B) 一般式 〔式中R5及びR6は水素原子または炭素数1
〜10のアルキル基、nは0ないし20の整数、m
は1または0、Yは炭素数3か4のα,β不飽
和モノカルボン酸の残基、そしてY′はmが0
のときは水素原子であり、mが1のときはYを
表わす〕 で表わされる化合物、または一般式 〔式中、n′は0ないし10の整数、R7は水素原
子または炭素数1〜10の炭化水素基そしてYは
炭素数3か4のα,β不飽和モノカルボン酸の
残基を表わす〕 で表わされる化合物3〜100重量部 (C) 300〜3000の分子量で50〜500のヨウ素価の炭
素−炭素二重結合および100g当り30〜300ミリ
モルのスルホン酸基あるいはコハク酸基を有す
る高分子化合物のマンガン塩0.2〜20重量部 よりなる低温硬化性の優れた陰極析出型電着塗料
組成物。
[Scope of Claims] 1 (A) A carbon-carbon double bond with a molecular weight of 500 to 10,000 and an iodine number of 50 to 500 and 30 to 100 grams per 100 g.
Polymer compound with 300 mmol of amino groups
100 parts by weight (B) General formula [In the formula, R 5 and R 6 are hydrogen atoms or carbon atoms 1
~10 alkyl group, n is an integer from 0 to 20, m
is 1 or 0, Y is the residue of an α,β unsaturated monocarboxylic acid having 3 or 4 carbon atoms, and Y′ is m is 0
When , it is a hydrogen atom, and when m is 1, it is Y.] A compound represented by or the general formula [In the formula, n' is an integer from 0 to 10, R 7 is a hydrogen atom or a hydrocarbon group having 1 to 10 carbon atoms, and Y represents a residue of an α,β unsaturated monocarboxylic acid having 3 or 4 carbon atoms. ] Compound 3 to 100 parts by weight (C) A polymer having a molecular weight of 300 to 3,000 and an iodine value of 50 to 500, a carbon-carbon double bond, and 30 to 300 mmol of sulfonic acid group or succinic acid group per 100 g. A cathodically deposited electrodeposition coating composition with excellent low temperature curability, comprising 0.2 to 20 parts by weight of a molecular compound manganese salt.
JP8007782A 1982-05-14 1982-05-14 Electrodeposition coating composition which deposits on cathode Granted JPS58198577A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP8007782A JPS58198577A (en) 1982-05-14 1982-05-14 Electrodeposition coating composition which deposits on cathode
US06/493,277 US4563501A (en) 1982-05-14 1983-05-10 Cathode-precipitating electrodeposition coating composition
EP83302677A EP0094788B1 (en) 1982-05-14 1983-05-11 Cathode-precipitating electrodeposition coating composition
DE8383302677T DE3366010D1 (en) 1982-05-14 1983-05-11 Cathode-precipitating electrodeposition coating composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8007782A JPS58198577A (en) 1982-05-14 1982-05-14 Electrodeposition coating composition which deposits on cathode

Publications (2)

Publication Number Publication Date
JPS58198577A JPS58198577A (en) 1983-11-18
JPH027338B2 true JPH027338B2 (en) 1990-02-16

Family

ID=13708144

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8007782A Granted JPS58198577A (en) 1982-05-14 1982-05-14 Electrodeposition coating composition which deposits on cathode

Country Status (1)

Country Link
JP (1) JPS58198577A (en)

Also Published As

Publication number Publication date
JPS58198577A (en) 1983-11-18

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