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JPH06211941A - Underwater antifouling coating composition - Google Patents

Underwater antifouling coating composition

Info

Publication number
JPH06211941A
JPH06211941A JP2364493A JP2364493A JPH06211941A JP H06211941 A JPH06211941 A JP H06211941A JP 2364493 A JP2364493 A JP 2364493A JP 2364493 A JP2364493 A JP 2364493A JP H06211941 A JPH06211941 A JP H06211941A
Authority
JP
Japan
Prior art keywords
ester
antifouling
oxalic acid
polymerization
oxalate
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.)
Pending
Application number
JP2364493A
Other languages
Japanese (ja)
Inventor
Hitoshi Tabuchi
均 田淵
Kiyomi Mori
喜代美 毛利
Toshiyuki Takesawa
利之 武澤
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.)
Nitto Kasei Co Ltd
Original Assignee
Nitto Kasei 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 Nitto Kasei Co Ltd filed Critical Nitto Kasei Co Ltd
Priority to JP2364493A priority Critical patent/JPH06211941A/en
Publication of JPH06211941A publication Critical patent/JPH06211941A/en
Pending legal-status Critical Current

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  • Paints Or Removers (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE:To obtain the subject composition capable of giving a coating film which can keep a suitable solubility in seawater for a long time by copolymerizing a specified crosslinking monomer with an ethylenically unsaturated monomer in the presence of a polymerization modifier. CONSTITUTION:100 pts.wt. monomer mixture comprising a cross-linking monomer of formula I (wherein X and Y are groups of formulas II-VI; R is H or methyl; (m) is 1-5; and (n) is 0-2) and other copolymerizable and ethylenically unsaturated monomers in the presence of 1-20 pts.wt. polymerization modifier to obtain a hydrolyzable resin composition of a weight-average molecular weight of 10000-100000. 5-200wt.% antifouling component is added to this composition to obtain the objective composition.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は加水分解性の良好な樹脂
組成物及び船舶、魚網などの水中構築物への海棲生物の
付着を防止するための防汚塗料組成物に関する。
TECHNICAL FIELD The present invention relates to a resin composition having good hydrolyzability and an antifouling coating composition for preventing marine organisms from adhering to underwater structures such as ships and fish nets.

【0002】[0002]

【従来の技術】トリ有機錫含有共重合体を用いた海中防
汚塗料は海水中で徐々に加水分解を受け、共重合体側鎖
のトリ有機錫部分が塗膜表面より徐々に溶出し、長期間
防汚効果を発揮できるので従来から広く使用されてい
た。
2. Description of the Related Art Submarine antifouling paints using a triorganotin-containing copolymer are gradually hydrolyzed in seawater, and the triorganotin portion of the side chain of the copolymer gradually elutes from the surface of the coating film. It has been widely used since it has an antifouling effect.

【0003】[0003]

【発明が解決しようとする課題】しかしトリ有機錫含有
共重合体を用いた海中防汚塗料は、近年海洋汚染の問題
から使用が制限されている。したがって環境汚染の心配
のない防汚塗料の開発が試みられているが、海中防汚塗
料の塗膜が海水中で充分に加水分解されないため、長期
間防汚性能を発揮できないのが現状である。
However, the use of marine antifouling paints using a triorganotin-containing copolymer has been restricted in recent years due to the problem of marine pollution. Therefore, attempts have been made to develop antifouling paints that do not worry about environmental pollution, but the present situation is that the antifouling performance of marine antifouling paints cannot be sufficiently hydrolyzed in seawater, so that they cannot exhibit antifouling performance for a long time. .

【0004】[0004]

【課題を解決するための手段】そこで本発明者等は鋭意
研究の結果、天然海水中で塗料塗膜の適度の溶解性を長
期間維持すると共に、海中防汚塗料として良好な塗膜物
性を有する樹脂組成物を見出し、本発明に至った。
[Means for Solving the Problems] Therefore, as a result of earnest research, the inventors of the present invention maintained an appropriate solubility of a coating film in natural seawater for a long period of time, and exhibited good coating properties as an underwater antifouling coating. The present invention has been completed, and the present invention has been completed.

【0005】すなわち本発明は、一般式〔4〕That is, the present invention has the general formula [4]

【化4】 で表される架橋性単量体を重合調整剤の存在下で、他の
共重合可能なエチレン性不飽和単量体と共重合させて得
られる加水分解性の樹脂組成物及び該樹脂組成物に防汚
成分を添加することを特徴とする海中防汚塗料組成物で
ある。
[Chemical 4] And a hydrolyzable resin composition obtained by copolymerizing a crosslinkable monomer represented by the above with another copolymerizable ethylenically unsaturated monomer in the presence of a polymerization modifier, and the resin composition An undersea antifouling coating composition, characterized in that an antifouling component is added to the composition.

【0006】本発明の加水分解性の樹脂組成物は、一般
式〔5〕
The hydrolyzable resin composition of the present invention has the general formula [5]

【化5】 (式中、X及びYは前記と同じ意義を有する)で表され
る架橋性不飽和単量体の1種又は2種以上を重合調整剤
の存在下で、他の共重合可能なエチレン性不飽和単量体
の1種又は2種以上と共重合することによって得られ
る。
[Chemical 5] (In the formula, X and Y have the same meanings as described above) One or more crosslinkable unsaturated monomers represented by another copolymerizable ethylenic group in the presence of a polymerization regulator are used. It is obtained by copolymerizing with one or more unsaturated monomers.

【0007】かかる共重合反応で重合調整剤を使用する
のは、一般式〔5〕で示される不飽和単量体が架橋性で
あるため、得られる共重合体がプリン状のゲル物質とな
り、加水分解性の塗料用樹脂組成物を供し得なくなるの
を防止することにある。
The polymerization modifier is used in such a copolymerization reaction, because the unsaturated monomer represented by the general formula [5] is crosslinkable, the resulting copolymer becomes a purine-like gel substance, The purpose is to prevent the hydrolyzable coating resin composition from becoming unusable.

【0008】一般式〔5〕で表わされる架橋性不飽和単
量体としては、架橋剤となり得るシュウ酸エステル、シ
ュウ酸アミドであれば特に限定されることはないが、例
えばシュウ酸ジビニルエステル、シュウ酸ジアリルエス
テル、シュウ酸ジアクリロイルオキシエチルエステル、
シュウ酸ジメタクリロイルオキシエチルエステル、シュ
ウ酸ジビニルオキシエチルエステル、シュウ酸ジビニル
オキシブチルエステル、シュウ酸ジアクリロイルオキシ
プロピルエステル、シュウ酸ジメタクリロイルオキシプ
ロピルエステル、シュウ酸ジ(2′−ビニルフェニル)
エステル、シュウ酸ジ(3′−ビニルフェニル)エステ
ル、シュウ酸ジ(4′−ビニルフェニル)エステル、
N,N′−ジアクリロイルオキシエチルシュウ酸アミ
ド、N,N′−ジメタクリロイルオキシエチルシュウ酸
アミド、シュウ酸ビニル(ビニルオキシエチル)エステ
ル、シュウ酸ビニル(ビニルオキシブチル)エステル、
シュウ酸ビニル(アクリロイルオキシエチル)エステ
ル、シュウ酸ビニル(メタクリロイルオキシエチル)エ
ステル、シュウ酸ビニル(2′−ビニルフェニル)エス
テル、シュウ酸ビニル(3′−ビニルフェニル)エステ
ル、シュウ酸ビニル(4′−ビニルフェニル)エステ
ル、シュウ酸アクリロイルオキシエチル(ビニルオキシ
エチル)エステル、シュウ酸メタクリロイルオキシエチ
ル(ビニルオキシエチル)エステル、シュウ酸アクリロ
イルオキシエチル(ビニルオキシブチル)エステル、シ
ュウ酸メタクリロイルオキシエチル(ビニルオキシブチ
ル)エステル、シュウ酸アクリロイルオキシエチル
(2′−ビニルフェニル)エステル、シュウ酸メタクリ
ロイルオキシエチル(2′−ビニルフェニル)エステ
ル、シュウ酸アクリロイルオキシエチル(3′−ビニル
フェニル)エステル、シュウ酸メタクリロイルオキシエ
チル(3′−ビニルフェニル)エステル、シュウ酸アク
リロイルオキシエチル(4′−ビニルフェニル)エステ
ル、シュウ酸メタクリロイルオキシエチル(4′−ビニ
ルフェニル)エステル、シュウ酸ビニル(アリル)エス
テル、シュウ酸アクリロイルオキシエチル(メタクリロ
イルオキシエチル)エステル、シュウ酸(2′−ビニル
フェニル)(3′−ビニルフェニル)エステル、シュウ
酸(2′−ビニルフェニル)(4′−ビニルフェニル)
エステル、シュウ酸(3′−ビニルフェニル)(4′−
ビニルフェニル)エステルなどが挙げられる。
The crosslinkable unsaturated monomer represented by the general formula [5] is not particularly limited as long as it is an oxalic acid ester or an oxalic acid amide which can serve as a crosslinking agent. For example, oxalic acid divinyl ester, Oxalic acid diallyl ester, oxalic acid diacryloyloxyethyl ester,
Oxalic acid dimethacryloyloxyethyl ester, oxalic acid divinyloxyethyl ester, oxalic acid divinyloxybutyl ester, oxalic acid diacryloyloxypropyl ester, oxalic acid dimethacryloyloxypropyl ester, oxalic acid di (2'-vinylphenyl)
Ester, oxalic acid di (3′-vinylphenyl) ester, oxalic acid di (4′-vinylphenyl) ester,
N, N′-diacryloyloxyethyl oxalic acid amide, N, N′-dimethacryloyloxyethyl oxalic acid amide, vinyl oxalate (vinyloxyethyl) ester, vinyl oxalate (vinyloxybutyl) ester,
Vinyl oxalate (acryloyloxyethyl) ester, vinyl oxalate (methacryloyloxyethyl) ester, vinyl oxalate (2′-vinylphenyl) ester, vinyl oxalate (3′-vinylphenyl) ester, vinyl oxalate (4 ′) -Vinylphenyl) ester, acryloyloxyethyl oxalate (vinyloxyethyl) ester, methacryloyloxyethyl oxalate (vinyloxyethyl) ester, acryloyloxyethyl oxalate (vinyloxybutyl) ester, methacryloyloxyethyl oxalate (vinyloxy) Butyl) ester, acryloyloxyethyl oxalate (2'-vinylphenyl) ester, methacryloyloxyethyl oxalate (2'-vinylphenyl) ester, acryloyl oxalate Ciethyl (3'-vinylphenyl) ester, methacryloyloxyethyl oxalate (3'-vinylphenyl) ester, acryloyloxyethyl oxalate (4'-vinylphenyl) ester, methacryloyloxyethyl oxalate (4'-vinylphenyl) Ester, vinyl (allyl) oxalate, acryloyloxyethyl (methacryloyloxyethyl) oxalate, oxalic acid (2'-vinylphenyl) (3'-vinylphenyl) ester, oxalic acid (2'-vinylphenyl) ( 4'-vinylphenyl)
Ester, oxalic acid (3'-vinylphenyl) (4'-
Vinyl phenyl) ester etc. are mentioned.

【0009】これらの架橋性不飽和単量体〔5〕は、シ
ュウ酸と酢酸ビニルとのエステル交換反応(ビニルエス
テルを調製する場合)若しくはシュウ酸ジクロリドと対
応するアルコ−ルとをトリエチルアミン、ピリジン、水
酸化ナトリウム、炭酸ナトリウム等の塩基の存在下で反
応することによって容易に得られる。
These crosslinkable unsaturated monomers [5] are obtained by transesterification of oxalic acid and vinyl acetate (when preparing vinyl ester) or oxalic acid dichloride and the corresponding alcohol with triethylamine and pyridine. It can be easily obtained by reacting in the presence of a base such as sodium hydroxide, sodium carbonate or the like.

【0010】一般式〔5〕で表わされる架橋性不飽和単
量体を共重合する場合の他のエチレン性不飽和単量体と
しては、共重合性がある単量体であれば限定されること
はないが、たとえばメチルメタクリレ−ト、エチルメタ
クリレ−ト、ブチルアクリレ−ト、2−エチルヘキシル
アクリレ−トなどのアクリル(メタクリル)酸エステ
ル、塩化ビニリデン、アクリロニトリル、アクリルアミ
ド、酢酸ビニル、N−ビニルピロリドンなどの官能基を
有するビニル系単量体、スチレン、ブタジエンなどのビ
ニル系炭化水素、マレイン酸ジメチル、イタコン酸ジメ
チルなどの不飽和ジカルボン酸ジエステルが挙げられ
る。
When the crosslinkable unsaturated monomer represented by the general formula [5] is copolymerized, the other ethylenically unsaturated monomer is limited as long as it is a copolymerizable monomer. However, acrylic (meth) acrylic acid esters such as methyl methacrylate, ethyl methacrylate, butyl acrylate, and 2-ethylhexyl acrylate, vinylidene chloride, acrylonitrile, acrylamide, vinyl acetate, N- Examples thereof include vinyl-based monomers having a functional group such as vinylpyrrolidone, vinyl-based hydrocarbons such as styrene and butadiene, and unsaturated dicarboxylic acid diesters such as dimethyl maleate and dimethyl itaconate.

【0011】本発明で用いる重合調整剤としては、例え
ばブチルメルカプタン、ラウリルメルカプタン、ドデシ
ルメルカプタン、チオグリコ−ル酸などの有機硫黄化合
物、2,4−ジフェニル−4−メチル−1−ペンテン
(α−メチルスチレンダイマ−)、1−メチル−4−イ
ソプロピリデン−シクロヘキセン(タ−ビノ−レン)な
どのスチレン誘導体が挙げられる。
Examples of the polymerization regulator used in the present invention include butyl mercaptan, lauryl mercaptan, dodecyl mercaptan, organic sulfur compounds such as thioglycolic acid, 2,4-diphenyl-4-methyl-1-pentene (α-methyl). Examples thereof include styrene derivatives such as styrene dimer) and 1-methyl-4-isopropylidene-cyclohexene (ta-binolene).

【0012】本発明中の一般式〔5〕で表わされる架橋
性不飽和単量体の使用量は、全重合性単量体100重量
部に対して1−20重量部であることが好ましい。1重
量部未満の使用量では、樹脂組成物の海水に対する加水
分解性が小さく、充分な防汚効果を発揮できず、また、
20重量部を超える使用量では、ゲル化を防止するため
に多量の重合調整剤、重合開始剤等を要し、経済上の観
点から好ましくないからである。
The amount of the crosslinkable unsaturated monomer represented by the general formula [5] used in the present invention is preferably 1 to 20 parts by weight based on 100 parts by weight of all the polymerizable monomers. If it is used in an amount of less than 1 part by weight, the resin composition has a low hydrolyzability in seawater and cannot exhibit a sufficient antifouling effect.
This is because if the amount used exceeds 20 parts by weight, a large amount of polymerization regulator, polymerization initiator, etc. are required to prevent gelation, which is not preferable from the economical viewpoint.

【0013】本発明で使用する重合調整剤の量は、全重
合性単量体100重量部に対して1−10重量部である
ことが好ましい。1重量部未満の使用では、重合反応を
調整する効果が不充分であり、10重量部を超えて使用
すれば、重合反応の進行が過度に阻害されるからであ
る。
The amount of the polymerization modifier used in the present invention is preferably 1-10 parts by weight based on 100 parts by weight of the total polymerizable monomers. This is because if the amount is less than 1 part by weight, the effect of adjusting the polymerization reaction is insufficient, and if the amount is more than 10 parts by weight, the progress of the polymerization reaction is excessively hindered.

【0014】本発明の樹脂組成物の重量平均分子量は1
0000−100000であることが望ましい。分子量
が10000未満であれば塗膜が脆弱となり、容易に剥
離する。一方分子量が100000を超えると重合溶液
の粘度が上昇し、取扱いが困難となるからである。
The weight average molecular weight of the resin composition of the present invention is 1
It is preferably 0000-100,000. If the molecular weight is less than 10,000, the coating film becomes brittle and easily peels off. On the other hand, if the molecular weight exceeds 100,000, the viscosity of the polymerization solution will increase and handling will be difficult.

【0015】つぎに本発明の海中防汚塗料組成物は、一
般式〔5〕で表わされる架橋性不飽和単量体を重合して
得られる加水分解性の樹脂組成物に防汚成分を添加する
ことを特徴とする防汚塗料組成物である。
Next, the marine antifouling coating composition of the present invention comprises an antifouling component added to a hydrolyzable resin composition obtained by polymerizing a crosslinkable unsaturated monomer represented by the general formula [5]. An antifouling coating composition characterized by the following.

【0016】防汚成分としては海棲汚損生物に対して殺
傷又は忌避作用を有する物質であれば限定されないが、
例えば亜酸化銅、ロダン銅、銅粉などの銅化合物、テト
ラクロルイソフタロニトリル、3,4−ジクロルフェニ
ルイソチオシアネ−トなどの有機化合物、ジチオカルバ
ミン酸亜鉛、2−メルカプトピリジンN−オキシド亜鉛
などの亜鉛化合物、チウラム系化合物、マレイミド系化
合物等が挙げられ、単独であるいは混合して使用でき
る。
The antifouling component is not limited as long as it is a substance having a killing or repelling action on marine fouling organisms,
For example, copper compounds such as cuprous oxide, copper rhodanide, and copper powder, organic compounds such as tetrachloroisophthalonitrile, 3,4-dichlorophenylisothiocyanate, zinc dithiocarbamate, and 2-mercaptopyridine N-oxide zinc. Examples thereof include zinc compounds, thiuram-based compounds, maleimide-based compounds, and the like, and these can be used alone or in a mixture.

【0017】本発明の海中防汚塗料組成物の防汚成分の
存在量は制限されないが、一般式〔5〕で表わされる架
橋性不飽和単量体を重合して得られる加水分解性の樹脂
組成物の5−200重量%が好ましい。
The amount of the antifouling component of the marine antifouling coating composition of the present invention is not limited, but a hydrolyzable resin obtained by polymerizing a crosslinkable unsaturated monomer represented by the general formula [5]. 5-200% by weight of the composition is preferred.

【0018】さらに本発明の海中防汚塗料には必要に応
じて、染料、顔料、可塑剤並びにロジン、塩化ゴム、ア
クリル樹脂、塩化ビニル−酢酸ビニル共重合体(VYH
H)などの天然または合成樹脂ビヒクルを併用すること
もできる。
Further, in the marine antifouling paint of the present invention, dyes, pigments, plasticizers, rosin, chlorinated rubber, acrylic resins, vinyl chloride-vinyl acetate copolymer (VYH) may be added, if necessary.
Natural or synthetic resin vehicles such as H) can also be used in combination.

【0019】[0019]

【実施例】次に実施例を挙げて本発明を説明するが、各
例中の%は重量%を、粘度は25℃での測定値を、分子
量はGPCによる重量平均分子量(ポリスチレン換算)
を示す。また合成単量体はIRおよびNMRにより目的
化合物であることを同定した。
EXAMPLES Next, the present invention will be described with reference to examples. In each example,% is% by weight, viscosity is the measured value at 25 ° C., and molecular weight is the weight average molecular weight by GPC (polystyrene conversion).
Indicates. The synthetic monomer was identified to be the target compound by IR and NMR.

【0020】1.不飽和単量体の製造 温度計、還流冷却器、攪拌器及び滴下ロ−トを備えた1
lの四ッ口フラスコに窒素気流中で2−ヒドロキシエチ
ルメタクリレ−ト156.2g(1.2mol)、ピリ
ジン94.9g(1.2mol)及びテトラヒドロフラ
ン(THF)400mlを入れ、氷冷下攪拌しながらシ
ュウ酸クロリド76.2g(0.6mol)を1時間か
けて滴下した。その後室温に戻して2時間攪拌した後、
反応液を濾過し、ピリジン塩酸塩を除いた後、濾液を減
圧下で濃縮した。得られた粗結晶をエタノ−ルから再結
晶してシュウ酸ジメタクリロイルオキシエチルエステル
142.6gを得た。収率は76%であった。同様な操
作により、シュウ酸ジアクリロイルオキシエチルエステ
ルを収率46%で、N,N′−ジメタクリロイルオキシ
エチルシュウ酸アミドを収率78%で、N,N′−ジア
クリロイルオキシエチルシュウ酸アミドを収率35%
で、シュウ酸ジ(4′−ビニルフェニル)エステルを収
率54%で得た。
1. Production of unsaturated monomer 1 equipped with thermometer, reflux condenser, stirrer and dropping funnel
In a nitrogen gas stream, 156.2 g (1.2 mol) of 2-hydroxyethyl methacrylate, 94.9 g (1.2 mol) of pyridine and 400 ml of tetrahydrofuran (THF) were placed in a four-necked flask of 1 l and stirred under ice cooling. Meanwhile, 76.2 g (0.6 mol) of oxalic acid chloride was added dropwise over 1 hour. After returning to room temperature and stirring for 2 hours,
The reaction solution was filtered to remove pyridine hydrochloride, and the filtrate was concentrated under reduced pressure. The obtained crude crystals were recrystallized from ethanol to obtain 142.6 g of dimethacryloyloxyethyl oxalate ester. The yield was 76%. By the same operation, oxalic acid diacryloyloxyethyl ester was obtained in a yield of 46%, N, N′-dimethacryloyloxyethyl oxalic acid amide was obtained in a yield of 78%, and N, N′-diacryloyloxyethyl oxalic acid amide was obtained. Yield 35%
Thus, oxalic acid di (4'-vinylphenyl) ester was obtained with a yield of 54%.

【0021】2.共重合体の製造 実施例1 温度計、還流冷却器及び攪拌器を備えた500mlの四
ッ口フラスコにシュウ酸ジメタクリロイルオキシエチル
エステル4g、メタクリル酸メチル92g、アクリル酸
ブチル100g、α−メチルスチレンダイマ−4g、キ
シレン200g及びアゾビスイソブチロニトリル(AI
BN)2gを入れ、窒素雰囲気下85−90℃で6時間
重合を行った。得られた共重合体溶液(共重合体溶液
A)は、粘度180cps、加熱残分47.4%で分子
量は30000であった。
2. Preparation of Copolymer Example 1 4 g of methacrylic acid dimethacryloyloxyethyl ester 4 g, methyl methacrylate 92 g, butyl acrylate 100 g, α-methylstyrene were placed in a 500 ml four-necked flask equipped with a thermometer, a reflux condenser and a stirrer. Dimer-4 g, xylene 200 g and azobisisobutyronitrile (AI
2 g of BN) was added, and polymerization was carried out at 85-90 ° C. for 6 hours in a nitrogen atmosphere. The obtained copolymer solution (copolymer solution A) had a viscosity of 180 cps, a heating residue of 47.4%, and a molecular weight of 30,000.

【0022】実施例2 温度計、還流冷却器及び攪拌器を備えた500mlの四
ッ口フラスコにシュウ酸ジアクリロイルオキシエチルエ
ステル10g、メタクリル酸メチル86g、アクリル酸
エチル104g、α−メチルスチレンダイマ−10g、
キシレン200g及びアゾビスイソブチロニトリル(A
IBN)4gを入れ、窒素雰囲気下85−90℃で6時
間重合を行った。得られた共重合体溶液(共重合体溶液
B)は、粘度150cps、加熱残分49.0%で分子
量は28000であった。
Example 2 In a 500 ml four-necked flask equipped with a thermometer, a reflux condenser and a stirrer, 10 g of oxalic acid diacryloyloxyethyl ester, 86 g of methyl methacrylate, 104 g of ethyl acrylate and α-methylstyrene dimer were added. 10g,
200 g of xylene and azobisisobutyronitrile (A
IBN) (4 g) was added, and polymerization was performed at 85-90 ° C. for 6 hours in a nitrogen atmosphere. The obtained copolymer solution (copolymer solution B) had a viscosity of 150 cps, a heating residue of 49.0%, and a molecular weight of 28,000.

【0023】実施例3 温度計、還流冷却器及び攪拌器を備えた500mlの四
ッ口フラスコにシュウ酸ジメタクリロイルオキシエチル
エステル4g、メタクリル酸メチル66g、アクリル酸
2−メトキシエチル130g、α−メチルスチレンダイ
マ−4g、キシレン200g及びアゾビスイソブチロニ
トリル(AIBN)2gを入れ、窒素雰囲気下85−9
0℃で6時間重合を行った。得られた共重合体溶液(共
重合体溶液C)は、粘度120cps、加熱残分49.
6%で分子量は28000であった。
Example 3 In a 500 ml four-necked flask equipped with a thermometer, a reflux condenser and a stirrer, 4 g of methacrylic acid dimethacryloyloxyethyl ester, 66 g of methyl methacrylate, 130 g of 2-methoxyethyl acrylate, and α-methyl were used. Styrene dimer-4 g, xylene 200 g, and azobisisobutyronitrile (AIBN) 2 g were put therein, and under a nitrogen atmosphere 85-9
Polymerization was carried out at 0 ° C. for 6 hours. The resulting copolymer solution (Copolymer solution C) had a viscosity of 120 cps and a heating residue of 49.
The molecular weight was 28,000 at 6%.

【0024】実施例4 温度計、還流冷却器及び攪拌器を備えた500mlの四
ッ口フラスコにN,N′−ジメタクリロイルオキシエチ
ルシュウ酸アミド20g、メタクリル酸イソブチル11
0g、アクリル酸ブチル50g、アクリル酸2−メトキ
シエチル20g、チオグリコ−ル酸20g、キシレン2
00g及びアゾビスイソブチロニトリル(AIBN)6
gを入れ、窒素雰囲気下85−90℃で6時間重合を行
った。得られた共重合体溶液(共重合体溶液D)は、粘
度100cps、加熱残分48.3%で分子量は220
00であった。
Example 4 In a 500 ml four-necked flask equipped with a thermometer, a reflux condenser and a stirrer, 20 g of N, N'-dimethacryloyloxyethyl oxalic acid amide and 11 of isobutyl methacrylate were used.
0 g, butyl acrylate 50 g, 2-methoxyethyl acrylate 20 g, thioglycolic acid 20 g, xylene 2
00g and azobisisobutyronitrile (AIBN) 6
g was added and polymerization was carried out at 85-90 ° C. for 6 hours in a nitrogen atmosphere. The obtained copolymer solution (Copolymer solution D) had a viscosity of 100 cps, a heating residue of 48.3%, and a molecular weight of 220.
It was 00.

【0025】実施例5 温度計、還流冷却器及び攪拌器を備えた500mlの四
ッ口フラスコにN,N′−ジアクリロイルオキシエチル
シュウ酸アミド2g、メタクリル酸メチル78g、メタ
クリル酸2−エトキシエチル20g、アクリル酸メチル
100g、ドデシルメルカプタン2g、キシレン200
g及びアゾビスイソブチロニトリル(AIBN)2gを
入れ、窒素雰囲気下85−90℃で6時間重合を行っ
た。得られた共重合体溶液(共重合体溶液E)は、粘度
190cps、加熱残分46.5%で分子量は1500
0であった。
Example 5 In a 500 ml four-necked flask equipped with a thermometer, a reflux condenser and a stirrer, 2 g of N, N'-diacryloyloxyethyl oxalic acid amide, 78 g of methyl methacrylate and 2-ethoxyethyl methacrylate were used. 20 g, methyl acrylate 100 g, dodecyl mercaptan 2 g, xylene 200
g and azobisisobutyronitrile (AIBN) (2 g) were added, and polymerization was carried out at 85-90 ° C. for 6 hours under a nitrogen atmosphere. The obtained copolymer solution (Copolymer solution E) had a viscosity of 190 cps, a heating residue of 46.5%, and a molecular weight of 1500.
It was 0.

【0026】実施例6 温度計、還流冷却器及び攪拌器を備えた500mlの四
ッ口フラスコにシュウ酸ジ(4′−ビニルフェニル)エ
ステル14g、マレイン酸ジブチル60g、酢酸ビニル
126g、α−メチルスチレンダイマ−10g、キシレ
ン200g及びアゾビスイソブチロニトリル(AIB
N)3gを入れ、窒素雰囲気下85−90℃で6時間重
合を行った。得られた共重合体溶液(共重合体溶液F)
は、粘度150cps、加熱残分47.3%で分子量は
30000であった。
Example 6 In a 500 ml four-necked flask equipped with a thermometer, a reflux condenser and a stirrer, 14 g of oxalic acid di (4'-vinylphenyl) ester, 60 g of dibutyl maleate, 126 g of vinyl acetate and α-methyl were used. Styrene dimer-10 g, xylene 200 g and azobisisobutyronitrile (AIB
N) (3 g) was added, and polymerization was carried out at 85-90 ° C. for 6 hours in a nitrogen atmosphere. Obtained copolymer solution (copolymer solution F)
Had a viscosity of 150 cps, a heating residue of 47.3%, and a molecular weight of 30,000.

【0027】比較例1 温度計、還流冷却器及び攪拌器を備えた500mlの四
ッ口フラスコにメタクリル酸メチル100g、アクリル
酸ブチル100g、キシレン200g及びアゾビスイソ
ブチロニトリル(AIBN)2gを入れ、窒素雰囲気下
85−90℃で6時間重合を行った。得られた共重合体
溶液(共重合体溶液G)は、粘度780cps、加熱残
分50.4%で分子量は40000であった。
Comparative Example 1 100 g of methyl methacrylate, 100 g of butyl acrylate, 200 g of xylene and 2 g of azobisisobutyronitrile (AIBN) were placed in a 500 ml four-necked flask equipped with a thermometer, a reflux condenser and a stirrer. Polymerization was carried out at 85-90 ° C. for 6 hours under a nitrogen atmosphere. The obtained copolymer solution (Copolymer solution G) had a viscosity of 780 cps, a heating residue of 50.4% and a molecular weight of 40,000.

【0028】比較例2 温度計、還流冷却器及び攪拌器を備えた500mlの四
ッ口フラスコにメタクリル酸イソブチル120g、アク
リル酸ブチル60g、アクリル酸2−メトキシエチル2
0g、キシレン200g及びアゾビスイソブチロニトリ
ル(AIBN)2gを入れ、窒素雰囲気下85−90℃
で6時間重合を行った。得られた共重合体溶液(共重合
体溶液H)は、粘度630cps、加熱残分49.8%
で分子量は54000であった。
Comparative Example 2 120 g of isobutyl methacrylate, 60 g of butyl acrylate, 2-methoxyethyl acrylate 2 were placed in a 500 ml four-necked flask equipped with a thermometer, a reflux condenser and a stirrer.
0 g, xylene 200 g and azobisisobutyronitrile (AIBN) 2 g were put, and the temperature was 85-90 ° C under a nitrogen atmosphere.
Polymerization was carried out for 6 hours. The resulting copolymer solution (copolymer solution H) had a viscosity of 630 cps and a heating residue of 49.8%.
And the molecular weight was 54,000.

【0029】3.海中防汚塗料の調製 (1)船底用海中防汚塗料の調製 実施例1−6で得た共重合体溶液A−F並びに比較例1
・2で得た共重合体溶液G・Hを用いて、下記第1表に
記載の配合成分を添加して本発明の船底用海中防汚塗料
を得た。配合結果を第1表に示す。なお表中の数字は重
量(g)を表わす。
3. Preparation of underwater antifouling paint (1) Preparation of undersea antifouling paint for ship bottoms Copolymer solutions AF obtained in Examples 1-6 and Comparative Example 1
Using the copolymer solutions G and H obtained in 2 above, the compounding ingredients shown in Table 1 below were added to obtain a marine antifouling paint for ship bottoms of the present invention. The compounding results are shown in Table 1. The numbers in the table represent weight (g).

【表1】 [Table 1]

【0030】(2)魚網用海中防汚塗料の調製 実施例1−6で得た共重合体溶液A−F並びに比較例1
・2で得た共重合体溶液G・Hを用いて、下記第2表に
記載の配合成分を添加して本発明の魚網用海中防汚塗料
を得た。配合結果を第2表に示す。なお表中の数字は重
量(g)を表わす。
(2) Preparation of undersea antifouling paint for fishnets Copolymer solutions AF obtained in Examples 1-6 and Comparative Example 1
Using the copolymer solutions G and H obtained in 2 above, the compounding ingredients shown in Table 2 below were added to obtain the undersea antifouling paint for fishnets of the present invention. The compounding results are shown in Table 2. The numbers in the table represent weight (g).

【表2】 [Table 2]

【0031】4.塗膜の溶解性試験 水槽の中央に直径318mm及び高さ440mmの回転
ドラムを取付け、これをモ−タ−で回転できるようにし
た。つぎに、海水の温度を一定に保つため加温装置及び
冷却装置を、また海水のPHを一定に保つためPH自動
コントロ−ラ−を取り付けた。実施例1−12及び比較
例1−4で得られた各共重合体及び海中防汚塗料を1m
m厚の硬質塩化ビニル板上に乾燥膜厚で約100ミクロ
ンとなるように塗布後、50℃で24時間乾燥させた。
海中防汚塗料を塗布した試験板を、上記の回転装置の回
転ドラムに海水と接触するように固定して、37km/
hrの速度で3箇月間海水中で回転させた。その期間中
海水の温度は25℃に、PHは8.0−8.2に保ち一
週間毎に海水を入れ換えた。各塗布試験板の初期の膜厚
と3箇月後の残存膜厚を顕微鏡で測定し、その差から溶
解した塗膜厚を計算した。結果を第3表に示す。
4. Solubility test of coating film A rotating drum having a diameter of 318 mm and a height of 440 mm was attached to the center of a water tank so that it could be rotated by a motor. Next, a heating device and a cooling device were attached to keep the temperature of the seawater constant, and a PH automatic controller was attached to keep the PH of the seawater constant. 1 m of each of the copolymers obtained in Example 1-12 and Comparative Example 1-4 and the marine antifouling paint
It was coated on a hard vinyl chloride plate having a thickness of m so that the dry film thickness was about 100 microns, and then dried at 50 ° C. for 24 hours.
The test plate coated with the undersea antifouling paint was fixed to the rotating drum of the above rotating device so as to come into contact with seawater, and 37 km /
It was spun in seawater for 3 months at a speed of hr. During that period, the temperature of seawater was kept at 25 ° C and the pH was kept at 8.0-8.2, and the seawater was replaced every week. The initial film thickness of each coating test plate and the remaining film thickness after 3 months were measured with a microscope, and the dissolved coating film thickness was calculated from the difference. The results are shown in Table 3.

【表3】 [Table 3]

【0032】5.防汚試験 (1)船底防汚試験 本発明の船底用海中防汚塗料組成物である実施例7−1
2及び比較例3・4を硬質塩化ビニル板の両面に乾燥膜
厚で200ミクロンになるように塗布した。この試験板
を三重県尾鷲湾の海面下1.5mに浸漬して付着生物に
よる試験板の汚損を18箇月間観察した。この結果を第
4表に示す。なお表中の数字は汚損生物の付着面積パ−
セントを表す。
5. Antifouling test (1) Ship bottom antifouling test Example 7-1 which is the undersea antifouling coating composition for ship bottoms of the present invention
2 and Comparative Examples 3 and 4 were coated on both sides of a hard vinyl chloride plate so that the dry film thickness would be 200 microns. The test plate was immersed 1.5 m below the sea surface in Owase Bay, Mie Prefecture, and the test plate was observed for contamination for 18 months. The results are shown in Table 4. The numbers in the table are the areas where the fouling organisms are attached.
Represents cents.

【表4】 [Table 4]

【0033】(2)魚網防汚試験 本発明の魚網用海中防汚塗料組成物である実施例13−
18及び比較例5・6にポリエチレン製魚網片(20c
m×20cm)を5分間浸した後、常温で1日乾燥し、
三重県尾鷲湾の海面下1.5mに浸漬して付着生物によ
る試験板の汚損を5箇月間観察した。この結果を下記の
評価基準に基づいて評価し、第5表にまとめた。 ◎:生物の付着がないか、スライムのみが付着してい
る。 ○:生物が僅かに付着するが、養殖網として支障がな
い。 △:生物の付着によって養殖網として使用に耐えられな
い程度である。 ×:生物が大量に付着している。
(2) Fishnet Antifouling Test Example 13- which is the undersea antifouling coating composition for fishnets of the present invention
18 and Comparative Examples 5 and 6 include polyethylene fish net pieces (20c
m × 20 cm) for 5 minutes, then dry at room temperature for 1 day,
The test plate was immersed in 1.5 m below the sea level in Owase Bay, Mie Prefecture, and the test plate was observed for contamination for 5 months. The results are evaluated based on the following evaluation criteria and summarized in Table 5. ⊚: No organism attached or only slime attached. ◯: A small amount of organisms adhere, but there is no problem as a culture net. Δ: The degree of being unusable as a culture net due to adhesion of organisms. X: A large amount of organisms are attached.

【表5】 [Table 5]

【0034】[0034]

【効果】重合調節剤の存在下で架橋性不飽和単量体を重
合して得られる本発明に係る加水分解性の樹脂組成物
は、天然海水中で樹脂中の架橋した部位が適度に崩壊す
るので、第3表に掲げる塗膜溶解性試験の結果からも明
らかなように、塗膜が長期間安定して溶解し続けるべく
適度の加水分解性を呈する。加えて、本発明の樹脂組成
物は船底、魚網等の基材に対する接着性に優れると共
に、その塗膜は強靱である。したがって当該樹脂組成物
に防汚成分を添加してなる本発明の海中防汚塗料組成物
は長期に渡って防汚効果を持続でき、塗料の貯蔵安定性
にも優れ、従来の防汚剤にみられるような海洋汚染の心
配もない。
[Effect] The hydrolyzable resin composition according to the present invention obtained by polymerizing a crosslinkable unsaturated monomer in the presence of a polymerization regulator is capable of appropriately disintegrating the crosslinked site in the resin in natural seawater. Therefore, as is clear from the results of the coating film solubility test shown in Table 3, the coating film exhibits an appropriate hydrolyzability so that it can be stably dissolved for a long period of time. In addition, the resin composition of the present invention has excellent adhesion to substrates such as ship bottoms and fish nets, and its coating film is tough. Therefore, the underwater antifouling coating composition of the present invention obtained by adding an antifouling component to the resin composition can maintain the antifouling effect for a long period of time, is excellent in the storage stability of the coating, and is a conventional antifouling agent. There is no worry of marine pollution as seen.

フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C09D 5/14 PQJ 6904−4J 125/00 PFB 9166−4J 129/10 PFP 6904−4J 131/04 PDT 6904−4J 133/00 PFY 7921−4J Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI Technical display location C09D 5/14 PQJ 6904-4J 125/00 PFB 9166-4J 129/10 PFP 6904-4J 131/04 PDT 6904- 4J 133/00 PPHY 7921-4J

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 一般式〔2〕 【化2】 で表される架橋性単量体を重合調整剤の存在下で、他の
共重合可能なエチレン性不飽和単量体と共重合させて得
られる加水分解性の樹脂組成物。
1. A general formula [2]: A hydrolyzable resin composition obtained by copolymerizing the crosslinkable monomer represented by the above with another copolymerizable ethylenically unsaturated monomer in the presence of a polymerization modifier.
【請求項2】 一般式〔3〕 【化3】 で表される架橋性単量体を重合調整剤の存在下で、他の
共重合可能なエチレン性不飽和単量体と共重合させて得
られる加水分解性の樹脂組成物に防汚成分を添加するこ
とを特徴とする海中防汚塗料組成物。
2. A general formula [3]: In the presence of a polymerization modifier, a crosslinkable monomer represented by a hydrolyzable resin composition obtained by copolymerizing with another copolymerizable ethylenically unsaturated monomer, an antifouling component. An underwater antifouling coating composition characterized by being added.
JP2364493A 1993-01-18 1993-01-18 Underwater antifouling coating composition Pending JPH06211941A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2364493A JPH06211941A (en) 1993-01-18 1993-01-18 Underwater antifouling coating composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2364493A JPH06211941A (en) 1993-01-18 1993-01-18 Underwater antifouling coating composition

Publications (1)

Publication Number Publication Date
JPH06211941A true JPH06211941A (en) 1994-08-02

Family

ID=12116271

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2364493A Pending JPH06211941A (en) 1993-01-18 1993-01-18 Underwater antifouling coating composition

Country Status (1)

Country Link
JP (1) JPH06211941A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009209291A (en) * 2008-03-05 2009-09-17 Toray Fine Chemicals Co Ltd Method for manufacturing acrylic copolymer
JP2010031159A (en) * 2008-07-30 2010-02-12 Toray Fine Chemicals Co Ltd Method for producing acrylic copolymer
CN104540684A (en) * 2012-08-27 2015-04-22 爱克发印艺公司 Free radical radiation curable liquids for de-inking substrates
CN112566989A (en) * 2018-08-29 2021-03-26 日东化成株式会社 Antifouling coating composition

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009209291A (en) * 2008-03-05 2009-09-17 Toray Fine Chemicals Co Ltd Method for manufacturing acrylic copolymer
JP2010031159A (en) * 2008-07-30 2010-02-12 Toray Fine Chemicals Co Ltd Method for producing acrylic copolymer
CN104540684A (en) * 2012-08-27 2015-04-22 爱克发印艺公司 Free radical radiation curable liquids for de-inking substrates
CN112566989A (en) * 2018-08-29 2021-03-26 日东化成株式会社 Antifouling coating composition
CN112566989B (en) * 2018-08-29 2022-02-15 日东化成株式会社 Antifouling coating composition

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