JP2882730B2 - Aqueous coating composition - Google Patents

Aqueous coating composition

Info

Publication number
JP2882730B2
JP2882730B2 JP17304493A JP17304493A JP2882730B2 JP 2882730 B2 JP2882730 B2 JP 2882730B2 JP 17304493 A JP17304493 A JP 17304493A JP 17304493 A JP17304493 A JP 17304493A JP 2882730 B2 JP2882730 B2 JP 2882730B2
Authority
JP
Japan
Prior art keywords
water
weight
acid
polymer
vinyl polymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP17304493A
Other languages
Japanese (ja)
Other versions
JPH0726195A (en
Inventor
誠 守屋
康敬 土井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP17304493A priority Critical patent/JP2882730B2/en
Publication of JPH0726195A publication Critical patent/JPH0726195A/en
Application granted granted Critical
Publication of JP2882730B2 publication Critical patent/JP2882730B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Paints Or Removers (AREA)
  • Inks, Pencil-Leads, Or Crayons (AREA)

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、優れた耐水性と、優れ
た顔料分散性とが両立した水性被覆用組成物に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an aqueous coating composition having both excellent water resistance and excellent pigment dispersibility.

【0002】[0002]

【従来の技術】近年、環境上の観点より、水系の被覆用
組成物のニーズは非常に高まっており、各種のものが開
発されている。
2. Description of the Related Art In recent years, from the viewpoint of the environment, the needs of aqueous coating compositions have been greatly increased, and various types of coating compositions have been developed.

【0003】エマルション、ディスパージョン等は、重
合体が水中に分散して存在するので、分子量が高くなっ
てもあまり大きな粘度上昇が生じないため、高分子量の
重合体を使用することが可能である。このため、塗装後
の塗膜物性が非常に良好な水性被覆用組成物を調製でき
るという利点が有り、これまで非常に多くのものが開発
されてきた。
[0003] Emulsions, dispersions, and the like, because polymers are dispersed in water, do not cause a significant increase in viscosity even when the molecular weight increases, so that a high molecular weight polymer can be used. . For this reason, there is an advantage that an aqueous coating composition having very good physical properties of a coated film after coating can be prepared, and a great many have been developed so far.

【0004】しかし、高濃度で顔料を分散させる必要の
ある場合には、重合体が顔料を包み込み顔料の再凝集を
防ぐという作用が不可欠であるが、重合体が水中に分散
して存在するエマルション、デイスパージョン等では、
顔料の再凝集が防ぎきれず、充分な顔料分散性が得られ
なかった。すなわち、顔料を包み込み顔料の再凝集を防
ぐためには、重合体が水中に溶解して存在することが必
要であり、このため従来より水溶性重合体の開発が種々
進められてきた。その代表例として、ポリビニルアルコ
ール、ポリアクリル酸のソーダー塩などが挙げられる。
[0004] However, when it is necessary to disperse the pigment at a high concentration, it is essential that the polymer wraps the pigment to prevent reaggregation of the pigment. , Dispersion, etc.,
Re-aggregation of the pigment could not be prevented, and sufficient pigment dispersibility could not be obtained. That is, in order to enclose the pigment and prevent re-aggregation of the pigment, it is necessary that the polymer is dissolved in water and exists. For this reason, various developments of water-soluble polymers have been conventionally made. Typical examples thereof include polyvinyl alcohol and a soda salt of polyacrylic acid.

【0005】しかし、これらの水溶性重合体は、塗膜の
形成後も重合体が水によく溶解する性格が残存しやすい
ため、水滴が落ちるなど非常に些細なことで塗膜が再溶
解し、ダメージを受けてしまうため、実用上不都合な点
が多かった。
However, since these water-soluble polymers tend to remain soluble in water even after the formation of the coating film, the coating film is re-dissolved due to trivial effects such as dropping of water droplets. However, there were many disadvantages in practical use due to damage.

【0006】この点を解決するためにスルフォン酸、カ
ルボン酸等の酸基を有する重合体を揮発性塩基により中
和し、塩とすることにより重合体を水中ヘ可溶化し、塗
装後の乾燥時に揮発性塩基が揮発することにより、水に
不溶化させるという手法に基づく水性被覆用組成物の開
発が近年多く紹介されている。
In order to solve this problem, a polymer having an acid group such as sulfonic acid and carboxylic acid is neutralized with a volatile base to form a salt, so that the polymer is solubilized in water and dried after coating. In recent years, many developments of aqueous coating compositions based on a technique of insolubilizing in water due to volatilization of a volatile base have been introduced in recent years.

【0007】例えば、特開昭60−215007号公報
には、連続混合反応域に特定方法で単量体等を供給して
重合させ分子量分布が狭く低分子量のアクリル系重合体
を製造する方法が開示されている。しかし、この方法で
は塩基により中和後水に溶解させることが可能な程度ま
で酸基を含む単量体を共重合すると、顔料分散性は非常
に良好であるが、耐水性が低下した。
[0007] For example, Japanese Patent Application Laid-Open No. 60-215007 discloses a method for producing a low molecular weight acrylic polymer having a narrow molecular weight distribution by supplying a monomer or the like to a continuous mixing reaction zone by a specific method and polymerizing the monomer. It has been disclosed. However, in this method, when a monomer containing an acid group is copolymerized to an extent that it can be dissolved in water after neutralization with a base, pigment dispersibility is very good, but water resistance is reduced.

【0008】このように、これまで開発された水性被覆
用組成物では、水中ヘの溶解性を高めるために、酸価を
高くせざるを得なかった。このため、塗膜表面に水滴を
たらし、指で5回こするなどすると、塗膜が溶けてしま
うなどの様な低位の耐水性ではなくなったが、水中に1
0時間放置するなど厳しい耐水性テストを受けると、塗
膜が白濁するなどの劣化の発生が避けられなかった。
As described above, in the aqueous coating composition thus far developed, the acid value has to be increased in order to increase the solubility in water. For this reason, when a water droplet is dropped on the surface of the coating film and rubbed five times with a finger, the coating film does not have a low level of water resistance such as dissolving, but the water is not immersed in water.
When subjected to a severe water resistance test such as being left for 0 hours, deterioration such as clouding of the coating film was unavoidable.

【0009】この塗膜の白濁等の劣化は、重合体の酸価
を低下させることにより改良可能である。しかし、重合
体の酸価を低下させると重合体の水中ヘの溶解性を急激
に低下させ、重合体が水中に分散した状態になってしま
い、顔料分散性を低下させてしまう。一部エマルション
等耐水性の良好の重合体分散物を重合体水性溶解物にブ
レンドする検討もされているが、高濃度で顔料を分散さ
せる必要のある場合にはやはり顔料分散性と耐水性のバ
ランスを両立させることが不可能であった。したがっ
て、酸価が低く耐水性が良好であり、かつ水中に良好に
溶解して優れた顔料分散性を示す水性被覆用組成物が要
望されていた。
The deterioration of the coating film such as cloudiness can be improved by lowering the acid value of the polymer. However, when the acid value of the polymer is reduced, the solubility of the polymer in water is rapidly reduced, and the polymer is dispersed in water, and the dispersibility of the pigment is reduced. Some polymer dispersions with good water resistance, such as emulsions, are also being studied for blending with aqueous polymer solutions.However, when it is necessary to disperse the pigment at a high concentration, It was impossible to balance. Accordingly, there has been a demand for an aqueous coating composition which has a low acid value and good water resistance, and which is well dissolved in water and exhibits excellent pigment dispersibility.

【0010】[0010]

【発明が解決しようとする課題】本発明の目的は、耐水
性に優れ、かつ顔料分散性にも優れた水性被覆用組成物
を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide an aqueous coating composition having excellent water resistance and excellent pigment dispersibility.

【0011】[0011]

【課題を解決するための手段】すなわち、本発明は、
(a)メチルメタクリレート30〜90重量%、(b)
芳香族ビニル化合物0〜30重量%、(c)酸基含有ビ
ニル化合物4〜15重量%および(d)共重合可能な他
のビニル系単量体0〜66重量%からなり、二次転移温
度が30〜100℃、重量平均分子量が7,000〜3
0,000、かつ酸価が30〜90mgKOH/gであ
り、懸濁重合法により重合されたビニル系重合体(I)
を、沸点が200℃以下の塩基でビニル系重合体(I)
の酸基の70〜100%を中和し、水中に溶解してなる
水性被覆用組成物である。
That is, the present invention provides:
(A) 30 to 90% by weight of methyl methacrylate, (b)
A secondary transition temperature comprising 0 to 30% by weight of an aromatic vinyl compound, 4 to 15% by weight of (c) an acid group-containing vinyl compound and 0 to 66% by weight of (d) another copolymerizable vinyl monomer. Is 30 to 100 ° C, and the weight average molecular weight is 7,000 to 3
000 and an acid value of 30 to 90 mgKOH / g.
Vinyl polymer (I) polymerized by a suspension polymerization method
Is a vinyl polymer (I) with a base having a boiling point of 200 ° C. or less.
Aqueous coating composition obtained by neutralizing 70 to 100% of the acid groups of the above and dissolving in water.

【0012】[0012]

【作用】本発明に用いられるビニル系重合体(I)は、
(a)メチルメタクリレート30〜90重量%、(b)
芳香族ビニル化合物0〜30重量%、(c)酸基含有ビ
ニル化合物4〜15重量%および(d)共重合可能な他
のビニル系単量体0〜66重量%から構成される。
The vinyl polymer (I) used in the present invention comprises:
(A) 30 to 90% by weight of methyl methacrylate, (b)
It is composed of 0 to 30% by weight of an aromatic vinyl compound, 4 to 15% by weight of (c) an acid group-containing vinyl compound, and 0 to 66% by weight of another copolymerizable vinyl monomer.

【0013】メチルメタクリレート(a)は、ビニル系
重合体に硬度を付与するための必須成分であり、30〜
90重量%の割合で用いられる。30重量%未満である
と硬度が低下し、一方90重量%を越えると水溶性が低
下する。
[0013] Methyl methacrylate (a) is an essential component for imparting hardness to the vinyl polymer.
It is used in a proportion of 90% by weight. If the amount is less than 30% by weight, the hardness decreases, while if it exceeds 90% by weight, the water solubility decreases.

【0014】芳香族ビニル化合物(b)は、塗膜に耐水
性を付与する効果があり、30重量%までの範囲で共重
合され、好ましくは0〜25重量%の範囲で使用され
る。しかし、30重量を越えると、水溶性が低下する
ので適当ではない。芳香族ビニル化合物の具体例として
は、スチレン、αーメチルスチレン、p−メチルスチレ
ンおよびベンジル(メタ)アクリレート等が挙げられる
が、なかでもスチレンが特に好ましい。
The aromatic vinyl compound (b) has an effect of imparting water resistance to the coating film, and is copolymerized in a range of up to 30% by weight, preferably in a range of 0 to 25% by weight. However, if it exceeds 30 % by weight, the water solubility is lowered, so that it is not suitable. Specific examples of the aromatic vinyl compound include styrene, α-methylstyrene, p-methylstyrene, and benzyl (meth) acrylate, among which styrene is particularly preferred.

【0015】酸基含有ビニル化合物(c)は、ビニル系
重合体に酸基を付与するものであり、カルボン酸または
スルフォン酸等の酸性基を有する化合物である。酸基含
有ビニル化合物は、4〜15重量%の範囲で得られるビ
ニル系重合体(I)の酸価が30〜90mgKOH/g
となるよう用いられる。酸基含有ビニル化合物の具体例
としては、アクリル酸、メタクリル酸、クロトン酸等の
一塩基酸;フマール酸、マレイン酸、イタコン酸などの
二塩基酸;およびこれらの部分エステル等が挙げられ
る。これらは二種以上を混合して使用することも可能で
ある。なかでもカルボン酸を有するビニル化合物を共重
合した場合には、水溶解性、耐水性および顔料分散性が
良好なものが得られる。また、特にメタクリル酸を共重
合した場合には、水溶解性、耐水性および顔料分散性が
いずれも非常に良好である。
The acid group-containing vinyl compound (c) imparts an acid group to the vinyl polymer and is a compound having an acidic group such as carboxylic acid or sulfonic acid. The acid value of the vinyl polymer (I) obtained in the range of 4 to 15% by weight is 30 to 90 mgKOH / g.
It is used so that Specific examples of the acid group-containing vinyl compound include monobasic acids such as acrylic acid, methacrylic acid and crotonic acid; dibasic acids such as fumaric acid, maleic acid and itaconic acid; and partial esters thereof. These can be used as a mixture of two or more kinds. In particular, when a vinyl compound having a carboxylic acid is copolymerized, a copolymer having good water solubility, water resistance and pigment dispersibility can be obtained. In particular, when methacrylic acid is copolymerized, water solubility, water resistance and pigment dispersibility are all very good.

【0016】また、上記単量体(a)〜(c)と共重合
可能な他のビニル系単量体(d)は、0〜66重量%の
範囲で用いられ、少なくとも一ケの重合可能なビニル基
を有するものの中から目的に応じて任意に選ぶことがで
きる。ビニル系単量体(d)の具体例としては、エチル
(メタ)アクリレート、n−ブチル(メタ)アクリレー
ト、i−ブチル(メタ)アクリレート、t−ブチル(メ
タ)アクリレート、シクロヘキシル(メタ)アクリレー
ト、2−エチルヘキシル(メタ)アクリレート、ラウリ
ル(メタ)アクリレート、ステアリル(メタ)アクリレ
ート等の炭素数1〜18のアルキル基を有する(メタ)
アクリル酸アルキルエステル;2−ヒドロキシエチル
(メタ)アクリレート、2−ヒドロキシプロピル(メ
タ)アクリレート等のヒドロキシアルキル(メタ)アク
リレート;エチレングリコールジ(メタ)アクリレー
ト、ブチレングリコール(メタ)アクリレート等のグリ
コールジ(メタ)アクリレート;ジメチルアミノエチル
(メタ)アクリレート等のアルキルアミノ(メタ)アク
リレート;およびジメチルアミノエチル(メタ)アクリ
レートメチルクロライド塩、シクロヘキシル(メタ)ア
クリレート、アリル(メタ)アクリレート、トリメチロ
ールプロパントリ(メタ)アクリレート、グリシジル
(メタ)アクリレート、酢酸ビニル、プロピオン酸ビニ
ル、(メタ)アクリロニトリル等が挙げられる。
The other vinyl monomer (d) copolymerizable with the monomers (a) to (c) is used in an amount of 0 to 66% by weight, and at least one polymerizable monomer is used. It can be arbitrarily selected from those having a suitable vinyl group according to the purpose. Specific examples of the vinyl monomer (d) include ethyl (meth) acrylate, n-butyl (meth) acrylate, i-butyl (meth) acrylate, t-butyl (meth) acrylate, cyclohexyl (meth) acrylate, (Meth) having an alkyl group having 1 to 18 carbon atoms, such as 2-ethylhexyl (meth) acrylate, lauryl (meth) acrylate, and stearyl (meth) acrylate
Alkyl acrylate; hydroxyalkyl (meth) acrylate such as 2-hydroxyethyl (meth) acrylate and 2-hydroxypropyl (meth) acrylate; glycol di (meth) acrylate such as ethylene glycol di (meth) acrylate and butylene glycol (meth) acrylate Meth) acrylates; alkylamino (meth) acrylates such as dimethylaminoethyl (meth) acrylate; and dimethylaminoethyl (meth) acrylate methyl chloride salt, cyclohexyl (meth) acrylate, allyl (meth) acrylate, trimethylolpropanetri (meth) acrylate ) Acrylate, glycidyl (meth) acrylate, vinyl acetate, vinyl propionate, (meth) acrylonitrile and the like.

【0017】ビニル系重合体(I)の二次転移温度は、
DSC法による測定で30〜100℃である必要があ
り、好ましくは35〜80℃である。30℃未満である
と耐汚染性が不足したり、耐ブロッキング性が低下す
る。また、100℃を越えると、塗膜が脆くなるという
欠点を示す。ビニル系重合体の分子量はGPC法により
測定される重量平均分子量が7,000〜30,000
である必要があり、好ましくは8,000〜25,00
0である。7,000未満では、塗膜が脆くなるという
欠点を示す。また、30,000を越えると、水溶性が
低下する。また、酸価は、フエノールフタレインの変色
点を基準としてビニル系重合体水溶液に、エタノールに
溶解したKOHを滴下して滴定し、ビニル系重合体1g
を中和するに必要なKOHのmg数で示した場合、35
〜90mgKOH/gである必要があり、好ましくは4
0〜70mgKOH/gである。35mgKOH/g未
満であると水溶解性が低下し、90mgKOH/gを越
えると耐水性が不足する。
The secondary transition temperature of the vinyl polymer (I) is as follows:
The temperature must be 30 to 100 ° C. as measured by the DSC method, and preferably 35 to 80 ° C. If the temperature is lower than 30 ° C., the stain resistance is insufficient or the blocking resistance is reduced. On the other hand, when the temperature exceeds 100 ° C., the coating film becomes brittle. The weight average molecular weight of the vinyl polymer measured by the GPC method is 7,000 to 30,000.
And preferably 8,000 to 25,000.
0. If it is less than 7,000, the coating film becomes brittle. On the other hand, when it exceeds 30,000, the water solubility decreases. The acid value was determined by adding KOH dissolved in ethanol dropwise to an aqueous solution of a vinyl polymer based on the discoloration point of phenolphthalein, and titrating the vinyl polymer.
When expressed in mg of KOH required to neutralize
9090 mg KOH / g, preferably 4
0-70 mgKOH / g. If it is less than 35 mgKOH / g, the solubility in water will decrease, and if it exceeds 90 mgKOH / g, the water resistance will be insufficient.

【0018】ビニル系重合体(I)を製造する際の重合
方法としては、懸濁重合法、溶液重合法、塊状重合法等
が適用できるが、特に懸濁重合法により製造されるもの
、耐水性に優れると同時に顔料分散性に優れるので、
本発明では懸濁重合法により製造したものを使用する。
また、重合を進行させながらモノマーを数度に分割して
系内に投入する方法や重合を進行させながらモノマーを
数時間かけて系内に滴下する重合方法により製造される
ものよりも、モノマーを一括して系内に投入した後に重
合を開始するモノマー一括仕込み方法により製造される
ものが好ましい。れは、共重合性の面からの効果であ
ると考えられる。
As the polymerization method for producing the vinyl polymer (I), a suspension polymerization method, a solution polymerization method, a bulk polymerization method and the like can be applied . Because it has excellent pigment dispersibility as well as excellent water resistance,
In the present invention, those produced by a suspension polymerization method are used.
In addition, rather than a method in which the monomer is divided into several degrees while the polymerization is proceeding and charged into the system or a method in which the monomer is dropped into the system over a period of several hours while the polymerization is proceeding, a method in which the monomer is produced is used. Those produced by a monomer batch charging method in which polymerization is started after the batch charging into the system are preferable. This is believed to be effective in terms of copolymerizability.

【0019】懸濁重合における分散剤としては、70〜
100%の範囲のケン化度のポバール、ポリメタクリル
酸のソーダー塩等公知の水溶性高分子を用いることがで
きる。また、溶液重合における溶剤としては、本発明で
用いる単量体および重合体を溶解させるものなら特に制
限を受けないが、メタノール、エタノール、イソプロピ
ルアルコール、n−ブタノールなどのアルコール類、エ
チルセルソルブ、セルソルブアセテート、ブチルカルビ
トール、プロピレングリコールメチルエーテル等のグリ
コール類、酢酸エチル、酢酸ブチルなどの酢酸エステル
類、メチルエチルケトン、メチルイソブチルケトンなど
のケトン類などが例として挙げられる。
As the dispersant in the suspension polymerization, 70 to
Known water-soluble polymers such as poval having a saponification degree in the range of 100% and a soda salt of polymethacrylic acid can be used. The solvent in the solution polymerization is not particularly limited as long as it dissolves the monomer and the polymer used in the present invention. However, alcohols such as methanol, ethanol, isopropyl alcohol and n-butanol, ethyl cellosolve, Examples thereof include glycols such as cellosolve acetate, butyl carbitol, and propylene glycol methyl ether; acetates such as ethyl acetate and butyl acetate; and ketones such as methyl ethyl ketone and methyl isobutyl ketone.

【0020】また、重合触媒としては、アゾビスイソブ
チロニトリル等のアゾ系開始剤、ベンゾイルパーオキサ
イド等の過酸化物系開始剤等従来公知の開始剤を目的に
応じて任意に使用することができる。
As the polymerization catalyst, conventionally known initiators such as azo initiators such as azobisisobutyronitrile and peroxide initiators such as benzoyl peroxide may be optionally used according to the purpose. Can be.

【0021】更に、ビニル系重合体(I)の分子量調節
用として、必要に応じて、上記ビニル系単量体混合物中
に、n−ドデシルメルカプタン、α−メチルスチレンダ
イマー等の連鎖移動剤を添加することができる。
If necessary, a chain transfer agent such as n-dodecyl mercaptan or α-methylstyrene dimer may be added to the above vinyl monomer mixture for controlling the molecular weight of the vinyl polymer (I). can do.

【0022】このようにして得られたビニル系重合体
(I)は、沸点200℃以下の塩基を用いてビニル系重
合体(I)中の酸基の70〜100%を中和して、塩を
形成することにより水溶性を付与し、水中に溶解され
る。ビニル系重合体の酸基の70%未満しか中和しない
場合は、重合体が水中に分散化するようになるため、顔
料分散性が不足する。
The vinyl polymer (I) thus obtained is neutralized with 70 to 100% of the acid groups in the vinyl polymer (I) using a base having a boiling point of 200 ° C. or less. By forming a salt, water solubility is imparted and the compound is dissolved in water. If less than 70% of the acid groups of the vinyl polymer are neutralized, the polymer will disperse in water, resulting in insufficient pigment dispersibility.

【0023】中和に用いる塩基は沸点が200℃以下の
ものであり、200℃を越えるものでは耐水性が低下す
る。沸点200℃以下の塩基の例としては、アンモニ
ア、トリエチルアミン、プロピルアミン、ジエチルアミ
ン、トリプロピルアミン、ジブチルアミン、アミルアミ
ン、1−アミノオクタン、2−ジメチルアミノエタノー
ル、エチルアミノエタノール、2−ジエチルアミノエタ
ノール、1−アミノ−2−プロパノール、2−アミノ−
1−プロパノール、3−アミノ−1−プロパノール、1
−ジメチルアミノ−2−プロパノール、3−ジメチルア
ミノ−1−プロパノール、2−プロピルアミノエタノー
ル、エトキシプロピルアミン、アミノベンジルアルコー
ル、モルホリン等が挙げられる。
The base used for the neutralization has a boiling point of 200 ° C. or less, and if it exceeds 200 ° C., the water resistance decreases. Examples of the base having a boiling point of 200 ° C. or lower include ammonia, triethylamine, propylamine, diethylamine, tripropylamine, dibutylamine, amylamine, 1-aminooctane, 2-dimethylaminoethanol, ethylaminoethanol, 2-diethylaminoethanol, -Amino-2-propanol, 2-amino-
1-propanol, 3-amino-1-propanol, 1
-Dimethylamino-2-propanol, 3-dimethylamino-1-propanol, 2-propylaminoethanol, ethoxypropylamine, aminobenzyl alcohol, morpholine and the like.

【0024】本発明の水性被覆用組成物は、上記ビニル
系重合体(I)の中和物を、通常20〜30重量%の濃
度で水に溶解したものとして用いられる。また、本発明
の水性被覆用組成物は、塗料およびインクとしての高度
の性能を発現させるために、消泡剤、顔料分散剤、防腐
剤等の添加剤を添加して用いることも可能である。
The aqueous coating composition of the present invention is used as a solution in which the neutralized product of the vinyl polymer (I) is dissolved in water at a concentration of usually 20 to 30% by weight. In addition, the aqueous coating composition of the present invention can be used by adding additives such as an antifoaming agent, a pigment dispersant, and a preservative in order to express high performance as a paint and an ink. .

【0025】本発明の水性被覆用組成物を用いて各種材
料の表面に塗膜を形成する際の塗布方法としては、噴霧
コート法、ローラーコート法、バーコート法、エアーナ
イフコート法、流延法、刷毛塗り法、ディッピング法等
が挙げられるが、特に限定されない。
The coating method for forming a coating on the surface of various materials using the aqueous coating composition of the present invention includes spray coating, roller coating, bar coating, air knife coating, and casting. Method, brush coating method, dipping method and the like, but are not particularly limited.

【0026】本発明の水性被覆用組成物を塗料として用
いる場合には、通常室温〜200℃の温度範囲で10秒
〜10時間乾燥して、塗膜が形成される。
When the aqueous coating composition of the present invention is used as a coating, it is dried usually at room temperature to 200 ° C. for 10 seconds to 10 hours to form a coating film.

【0027】[0027]

【実施例】以下に、本発明を実施例により詳細に説明す
る。なお、実施例中の「部」および「%」は、それぞれ
「重量部」および「重量%」を示す。 (1)ビニル系重合体I−1の製造 攪拌機、温度計、還流凝縮器を備えて、加温と冷却がい
ずれも可能である重合装置中に脱イオン水200部にポ
リビニルアルコール(ケン化度80%、重合度1,70
0)0.6部を加え、攪拌を行いポリビニルアルコール
を完全に溶解した後に、一度攪拌を停止し、メチルメタ
クリレート(以下、MMAと略)70部、スチレン(以
下、Stと略)10部、n−ブチルアクリレート(以
下、n−BAと略)10部、メタクリル酸(以下、MA
Aと略)10部を加え再度攪拌を開始し、アゾビスイソ
ブチロニトリル(以下、AIBNと略)0.5部および
n−ドデシルメルカプタン(以下、n−DMと略)4部
を加え75℃に昇温し、反応温度を75〜80℃を維持
するように3時間反応させ、その後95℃に昇温し1時
間維持し反応を終了させた。得られた重合体は、分子量
12,000、酸価65mgKOH/g、二次転移温度
87℃であった。 (2)ビニル系重合体I−2〜I−9の製造 ビニル系重合体I−1の製造方法と同様の操作で、表1
に示すビニル系単量体組成物を表1に示すラジカル開始
剤および連鎖移動剤を用いてそれぞれ重合し、得られた
重合体の特性値を表2に示した。
The present invention will be described below in detail with reference to examples. In the examples, “parts” and “%” indicate “parts by weight” and “% by weight”, respectively. (1) Production of vinyl polymer I-1 In a polymerization apparatus equipped with a stirrer, a thermometer, and a reflux condenser and capable of both heating and cooling, 200 parts of deionized water was mixed with polyvinyl alcohol (degree of saponification). 80%, degree of polymerization 1,70
0) After adding 0.6 part and stirring to completely dissolve the polyvinyl alcohol, the stirring was stopped once, and 70 parts of methyl methacrylate (hereinafter abbreviated as MMA), 10 parts of styrene (hereinafter abbreviated as St), n-butyl acrylate (hereinafter abbreviated as n-BA) 10 parts, methacrylic acid (hereinafter MA)
A) (10 parts) was added and stirring was started again, and 0.5 parts of azobisisobutyronitrile (hereinafter abbreviated as AIBN) and 4 parts of n-dodecylmercaptan (hereinafter abbreviated as n-DM) were added and added. C., and the reaction was carried out for 3 hours so that the reaction temperature was maintained at 75 to 80.degree. C., and then the temperature was raised to 95.degree. C. and maintained for 1 hour to terminate the reaction. The obtained polymer had a molecular weight of 12,000, an acid value of 65 mgKOH / g, and a secondary transition temperature of 87 ° C. (2) Production of vinyl polymers I-2 to I-9 Table 1 was prepared in the same manner as in the production method of vinyl polymer I-1.
Are polymerized using the radical initiator and the chain transfer agent shown in Table 1, respectively, and the characteristic values of the obtained polymer are shown in Table 2.

【0028】[0028]

【表1】 記号の説明 BPO:べンゾイルパーオキサイド n−BMA:ノルマルブチルメタクリレート EHA:エチルヘキシルアクリレート MeSt:α−メチルスチレンダイマー AA:アクリル酸[Table 1] Explanation of symbols BPO: benzoyl peroxide n-BMA: normal butyl methacrylate EHA: ethylhexyl acrylate MeSt: α-methylstyrene dimer AA: acrylic acid

【0029】[0029]

【表2】 (3)ビニル系重合体I−10の製造 攪拌機、温度計、還流凝縮器を備えて、加温と冷却がい
ずれも可能である重合装置中にイソプロピルアルコール
(以下、i−PAと略)100部、MMA65部、St
10部、n−BA12部、MAA13部、AIBN2部
およびn−DM3部を加え攪拌を開始し、80℃に昇温
し重合を開始し、1時間おきにAIBNを0.2部添加
し、9時間温度を維持し重合を終了し、固形分51%、
粘度10,000cpsのビニル系重合体のi−PA溶
液を得た。その後この溶液をバットに入れ、50℃に加
熱した乾燥機中にてi−PAを蒸発させ固形分99.5
%のビニル系重合体の固形物を得た。得られた重合体は
分子量13,000、酸価85.5mgKOH/g、二
次転移温度84℃であった。 (4)ビニル系重合体I−11の製造 攪拌機、温度計、還流凝縮器を備えて、加温と冷却がい
ずれも可能である重合装置中にi−PA100部を加え
攪拌を開始し、80℃に昇温しMMA65部、St10
部、n−BA12部、MAA13部、AIBN3部の混
合物を4時間かけて滴下し、その後1時間おきにAIB
Nを0.1部添加しながら4時間温度を維持して重合を
終了し、固形分50%、粘度2,000cpsのビニル
系重合体のi−PA溶液を得た。その後この溶液をバッ
トに入れ、50℃に加熱した乾燥機中にてi−PAを蒸
発させ固形分99.5%のビニル系重合体の固形物を得
た。得られた重合体は分子量11,000、酸価85.
5mgKOH/g、二次転移温度84℃であった。 (5)ビニル系重合体の水中ヘの溶解 〔5−1〕塩基としてアンモニアを用い、酸基を100
%中和する場合 攪拌機、温度計、還流凝縮器を備えて、加温と冷却がい
ずれも可能である300mlフラスコ中にビニル系重合
体I−1を50gおよび脱イオン水147.5gを投入
し攪拌を開始し、28%アンモニア水3.5gを徐々に
添加し、その後50℃に昇温し2時間温度を維持し溶解
を完了し、ビニル系重合体I−1の水性溶解物を得た。
得られた水性溶解物は固形分25%、粘度500cpS
であった。ビニル系重合体I−3〜I−11も下記の計
算方法に従い28%アンモニア水と脱イオン水の添加量
を計算し、同様の方法で溶解操作を行った。しかし、ビ
ニル系重合体I−6、I−8およびI−9は溶解できな
かった。 必要アンモニア水(g)=A÷56.1÷1000×5
0×l7÷0.28 (式中、Aは重合体の酸価(mgKOH/g)を表わ
す。) 必要脱イオン水(g)=150−必要アンモニア水
(g)×0.72 〔5−2〕塩基として2−ジメチルアミノエタノールを
用い、酸基を100%中和する場合 〔5−1〕と同様のフラスコ中にビニル系重合体I−3
を50gおよび脱イオン水150gを投入し攪拌を開始
し、2−ジメチルアミノエタノール7.9gを徐々に添
加し、その後50℃に昇温し2時間温度を維持し溶解を
完了し、ビニル系重合体I−3の水性溶解物を得た。得
られた水性溶解物は固形分25%、粘度70cpsであ
った。 〔5−3〕塩基としてジエタノールアミンを用い、酸基
を100%中和する場合 〔5−1〕と同様のフラスコ中にビニル系重合体I−1
を50gおよび脱イオン水150gを投入し撹幹を開始
し、ジエタノールアミン7gを徐々に添加し、その後5
0℃に昇温し2時間温度を維持し溶解を完了し、ビニル
系重合体I−1の水性溶解物を得た。得られた水性溶解
物は固形分25%、粘度100CpSであった。 〔5−4〕塩基としてアンモニアを用い、酸基を74%
中和する場合 〔5−1〕と同様のフラスコ中にビニル系重合体I−2
を50gおよび脱イオン水148.8gを投入し攪拌を
開始し、28%アンモニア水1.8gを徐々に添加し、
その後50℃に昇温し2時間温度を維持し溶解を完了
し、ビニル系重合体I−2の水性溶解物を得た。得られ
た水性溶解物は固形分25%、粘度90cpsであっ
た。 〔5−5〕塩基がアンモニア、酸を60%中和する場合 〔5−1〕と同様のフラスコ中にビニル系重合体I−1
を50gおよび脱イオン水148.5gを投入し攪拌を
開始し、28%アンモニア水2.1gを徐々に添加し、
その後50℃に昇温し2時間温度を維持し溶解を完了
し、ビニル系重合体I−1の水性溶解物を得た。得られ
た水性溶解物は固形分25%、粘度150cpsであっ
た。
[Table 2] (3) Production of Vinyl Polymer I-10 Isopropyl alcohol (hereinafter abbreviated as i-PA) 100 in a polymerization apparatus equipped with a stirrer, a thermometer, and a reflux condenser and capable of both heating and cooling. Part, MMA 65 parts, St
10 parts, 12 parts of n-BA, 13 parts of MAA, 2 parts of AIBN and 3 parts of n-DM were added, stirring was started, the temperature was raised to 80 ° C., polymerization was started, and 0.2 parts of AIBN was added every one hour. The temperature was maintained for a time to complete the polymerization, and the solid content was 51%.
An i-PA solution of a vinyl polymer having a viscosity of 10,000 cps was obtained. Thereafter, the solution was put into a vat, and i-PA was evaporated in a dryer heated to 50 ° C. to obtain a solid content of 99.5.
% Of a vinyl polymer solid. The obtained polymer had a molecular weight of 13,000, an acid value of 85.5 mgKOH / g, and a secondary transition temperature of 84 ° C. (4) Production of Vinyl Polymer I-11 100 parts of i-PA was added to a polymerization apparatus equipped with a stirrer, a thermometer, and a reflux condenser and capable of heating and cooling, and stirring was started. ℃ 65, MMA 65 parts, St10
, 12 parts of n-BA, 13 parts of MAA, and 3 parts of AIBN were added dropwise over 4 hours.
The polymerization was terminated by maintaining the temperature for 4 hours while adding 0.1 part of N to obtain an i-PA solution of a vinyl polymer having a solid content of 50% and a viscosity of 2,000 cps. Thereafter, the solution was put in a vat, and i-PA was evaporated in a dryer heated to 50 ° C. to obtain a vinyl polymer solid having a solid content of 99.5%. The resulting polymer had a molecular weight of 11,000 and an acid value of 85.
The secondary transition temperature was 5 mgKOH / g and the second transition temperature was 84 ° C. (5) Dissolution of vinyl polymer in water [5-1] Using ammonia as a base,
% Neutralization 50 g of vinyl polymer I-1 and 147.5 g of deionized water are charged into a 300 ml flask equipped with a stirrer, a thermometer, and a reflux condenser and capable of both heating and cooling. Stirring was started, and 3.5 g of 28% aqueous ammonia was gradually added. Thereafter, the temperature was raised to 50 ° C., and the temperature was maintained for 2 hours to complete the dissolution, thereby obtaining an aqueous solution of vinyl polymer I-1. .
The obtained aqueous solution has a solid content of 25% and a viscosity of 500 cpS.
Met. For the vinyl polymers I-3 to I-11, the addition amounts of 28% ammonia water and deionized water were calculated according to the following calculation method, and the dissolution operation was performed in the same manner. However, the vinyl polymers I-6, I-8 and I-9 could not be dissolved. Required ammonia water (g) = A ÷ 56.1 ÷ 1000 × 5
0 × 17 ÷ 0.28 (where A represents the acid value of the polymer (mg KOH / g).) Required deionized water (g) = 150−Necessary ammonia water (g) × 0.72 [5- 2] When 2-dimethylaminoethanol is used as the base and the acid groups are neutralized by 100% In the same flask as in [5-1], the vinyl polymer I-3 is placed.
Of 50 g of deionized water and 150 g of deionized water, and stirring was started. Then, 7.9 g of 2-dimethylaminoethanol was gradually added. An aqueous solution of coalescence I-3 was obtained. The obtained aqueous solution had a solid content of 25% and a viscosity of 70 cps. [5-3] When diethanolamine is used as a base and the acid group is neutralized by 100% The vinyl polymer I-1 is placed in the same flask as in [5-1].
And 50 g of deionized water were added thereto, stirring was started, and 7 g of diethanolamine was gradually added.
The temperature was raised to 0 ° C., and the temperature was maintained for 2 hours to complete the dissolution, thereby obtaining an aqueous solution of the vinyl polymer I-1. The obtained aqueous solution had a solid content of 25% and a viscosity of 100 CpS. [5-4] Using ammonia as a base and reducing acid groups by 74%
Neutralization In the same flask as in [5-1], place the vinyl polymer I-2 in the same flask.
Was added, and 508.8 g of deionized water and 148.8 g of deionized water were added thereto, stirring was started, and 1.8 g of 28% ammonia water was gradually added.
Thereafter, the temperature was raised to 50 ° C., and the temperature was maintained for 2 hours to complete the dissolution, thereby obtaining an aqueous solution of the vinyl polymer I-2. The resulting aqueous melt had a solids content of 25% and a viscosity of 90 cps. [5-5] When the base neutralizes ammonia and acid by 60% The vinyl polymer I-1 is placed in the same flask as in [5-1].
Was added, 50 g of deionized water and 148.5 g of deionized water were added, stirring was started, and 2.1 g of 28% ammonia water was gradually added.
Thereafter, the temperature was raised to 50 ° C., and the temperature was maintained for 2 hours to complete the dissolution, thereby obtaining an aqueous solution of the vinyl polymer I-1. The obtained aqueous solution had a solid content of 25% and a viscosity of 150 cps.

【0030】実施例1 Degussa製カーボンブラック#100をビニル系
重合体I−1の水性溶解物100部に対して20部加
え、FRITSCH製遊星ボールミルにて2時間ミキシ
ングし、顔料分散させた。その後100日間室温にて放
置したところ、顔料の沈降は見られなかった。また、顔
料分散直後ガラス板にソリッド膜厚80μmになるよう
塗布し、50℃の乾燥炉で20分乾燥後20℃の温水中
に10日間放置したところ、白化等のダメージは見られ
なかった。
Example 1 20 parts of carbon black # 100 manufactured by Degussa was added to 100 parts of the aqueous solution of the vinyl polymer I-1, and the mixture was mixed with a planetary ball mill manufactured by FRITSCH for 2 hours to disperse the pigment. Thereafter, when the mixture was left at room temperature for 100 days, no sedimentation of the pigment was observed. Immediately after the pigment was dispersed, the composition was applied to a glass plate so as to have a solid film thickness of 80 μm, dried in a drying oven at 50 ° C. for 20 minutes, and then left in warm water at 20 ° C. for 10 days. No damage such as whitening was observed.

【0031】 実施例2〜および比較例1〜 実施例1と同様にして試験を行った結果を表3に示し
た。なお、各試験の評価は下記の基準によった。 〔水溶解性〕前記(5)ビニル系重合体の溶解に準じて
水中に溶解させた。 良好:10時間後に層分離または沈殿を生じない。 不良:10時間後に層分離または沈殿を生じる。 〔顔料分散性〕Degussa製カーボンブラック#1
00をビニル系重合体の水性溶解物100部に対して2
0部加え、FRITSCH製遊星ボールミルにて2時間
ミキシングし、顔料分散させた。その後100日間室温
にて放置した。良好:顔料の沈降が見られない。 やや良好:100日後に顔料の沈降が見られる。 普通:30日後に顔料の沈降が見られる。(実用可能な
範囲) 不良:3日後に顔料の沈降が見られる。 〔耐水性〕顔料分散直後にガラス板にソリッド膜厚80
μmになるよう塗布し、50℃の乾燥炉で20分乾燥後
20℃の温水中に10日間放置した。 良好:白化等のダメージが見られない。 やや良好:10日後に白化、フクレ等のダメージが見ら
れる。 普通:3日後に白化、フクレ等のダメージが見られる。
(実用可能な範囲) 不良:5時間後に白化、フクレ等のダメージが見られ
る。
Examples 2 to 5 and Comparative Examples 1 to 8 Table 3 shows the results of tests performed in the same manner as in Example 1. The evaluation of each test was based on the following criteria. [Water solubility] The vinyl polymer was dissolved in water in the same manner as in (5) above. Good: no layer separation or precipitation occurs after 10 hours. Poor: Layer separation or precipitation occurs after 10 hours. [Pigment dispersibility] Carbon black # 1 manufactured by Degussa
00 with respect to 100 parts of the aqueous solution of the vinyl polymer.
0 parts were added and mixed for 2 hours with a FRITSCH planetary ball mill to disperse the pigment. Then, it was left at room temperature for 100 days. Good: No sedimentation of the pigment was observed. Moderately good: pigment sedimentation is observed after 100 days. Normal: pigment settling is observed after 30 days. (Usable range) Poor: Settling of pigment is observed after 3 days. [Water resistance] Solid film thickness of 80 on glass plate immediately after pigment dispersion
It was applied to a thickness of μm, dried in a drying oven at 50 ° C. for 20 minutes, and then left in warm water at 20 ° C. for 10 days. Good: No damage such as whitening is observed. Slightly good: Damage such as whitening and blistering is observed after 10 days. Normal: Damage such as whitening and blistering is observed after 3 days.
(Practically usable range) Poor: Damage such as whitening and blistering is observed after 5 hours.

【0032】[0032]

【表3】 [Table 3]

【0033】[0033]

【発明の効果】本発明の水性被覆用組成物は、耐水性に
優れると同時に顔料分散性にも優れ、これまで両者の両
立が不可能であった有機溶剤を含まない水性被覆用組成
物において、その効果は極めて顕著である。
Industrial Applicability The aqueous coating composition of the present invention is excellent in water resistance and pigment dispersibility, and is used in an aqueous coating composition containing no organic solvent, which has heretofore been incompatible with both. The effect is extremely remarkable.

フロントページの続き (56)参考文献 特開 平4−153276(JP,A) 特開 昭50−122528(JP,A) 特開 平4−57856(JP,A) 特開 昭51−7033(JP,A) 特開 昭53−37733(JP,A) 特開 平3−192172(JP,A) 特開 昭62−135575(JP,A) 特表 平3−504138(JP,A) (58)調査した分野(Int.Cl.6,DB名) C09D 133/04 - 133/14 C09D 5/00,11/10 C08L 33/04 - 33/14 Continuation of front page (56) References JP-A-4-153276 (JP, A) JP-A-50-122528 (JP, A) JP-A-4-57856 (JP, A) JP-A-51-7033 (JP, A) JP-A-53-37733 (JP, A) JP-A-3-192172 (JP, A) JP-A-62-135575 (JP, A) JP-A-3-504138 (JP, A) (58) Field surveyed (Int.Cl. 6 , DB name) C09D 133/04-133/14 C09D 5/00, 11/10 C08L 33/04-33/14

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 (a)メチルメタクリレート30〜90
重量%、(b)芳香族ビニル化合物0〜30重量%、
(c)酸基含有ビニル化合物4〜15重量%および
(d)共重合可能な他のビニル系単量体0〜66重量%
からなり、二次転移温度が30〜100℃、重量平均分
子量が7,000〜30,000、かつ酸価が30〜9
0mgKOH/gであり、懸濁重合法により重合された
ビニル系重合体(I)を、沸点が200℃以下の塩基で
ビニル系重合体(I)の酸基の70〜100%を中和
し、水中に溶解してなる水性被覆用組成物。
(A) methyl methacrylate 30 to 90
% By weight, (b) 0 to 30% by weight of an aromatic vinyl compound,
(C) 4 to 15% by weight of an acid group-containing vinyl compound and (d) 0 to 66% by weight of another copolymerizable vinyl monomer.
Having a secondary transition temperature of 30 to 100 ° C, a weight average molecular weight of 7,000 to 30,000, and an acid value of 30 to 9
0 mgKOH / g der is, polymerized <br/> vinyl polymer by suspension polymerization (I), a boiling point of 200 ° C. or less of the base of the acid groups of the vinyl polymer (I) 70 to 100 % Of an aqueous coating composition which is neutralized and dissolved in water.
【請求項2】 酸基含有ビニル化合物(c)が、メタク
リル酸を含むものである請求項1記載の水性被覆用組成
物。
2. The aqueous coating composition according to claim 1, wherein the acid group-containing vinyl compound (c) contains methacrylic acid.
JP17304493A 1993-07-13 1993-07-13 Aqueous coating composition Expired - Lifetime JP2882730B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17304493A JP2882730B2 (en) 1993-07-13 1993-07-13 Aqueous coating composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17304493A JP2882730B2 (en) 1993-07-13 1993-07-13 Aqueous coating composition

Publications (2)

Publication Number Publication Date
JPH0726195A JPH0726195A (en) 1995-01-27
JP2882730B2 true JP2882730B2 (en) 1999-04-12

Family

ID=15953171

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17304493A Expired - Lifetime JP2882730B2 (en) 1993-07-13 1993-07-13 Aqueous coating composition

Country Status (1)

Country Link
JP (1) JP2882730B2 (en)

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50122528A (en) * 1974-03-13 1975-09-26
IT1035831B (en) * 1974-06-03 1979-10-20 Ford Motor Co IMPROVEMENT IN THE PRODUCTION PROCESS OF WATER DISPERSION OF PAINTS AND PRODUCT OBTAINED USEFUL IN PARTICULAR FOR SPRAY APPLICATION
US4062823A (en) * 1976-09-20 1977-12-13 Ford Motor Company Hybrid water-based enamels with partially crosslinked latexes
DE3834738A1 (en) * 1988-10-12 1990-04-19 Basf Lacke & Farben METHOD FOR PRODUCING A MULTI-LAYER COATING, AQUEOUS COATING COMPOSITION, WATER-DISCOVERABLE POLYACRYLATE RESINS AND METHOD FOR PRODUCING WATER-DISCOVERABLE POLYACRYLATE RESINS
JP2717866B2 (en) * 1989-12-22 1998-02-25 ダイセル化学工業株式会社 Coating composition and coating film
JP2859705B2 (en) * 1990-06-27 1999-02-24 三菱レイヨン株式会社 Coating composition for paper polishing
JP2527271B2 (en) * 1990-10-16 1996-08-21 日立化成工業株式会社 Negative photosensitive electrodeposition coating resin composition and electrodeposition coating bath using the same

Also Published As

Publication number Publication date
JPH0726195A (en) 1995-01-27

Similar Documents

Publication Publication Date Title
JPH049182B2 (en)
JPH05117344A (en) Core-shell emulsion and aqueous press varnish using the same emulsion
JP2000080288A (en) Polymer dispersoid
JP2554401B2 (en) Aqueous resin dispersion and coating resin composition
JP2896833B2 (en) Vinyl polymer particles
CA3032277A1 (en) Ambient self-crosslinkable latex
JP2882732B2 (en) Aqueous coating composition
PT1325088E (en) Aqueous dispersion of addition polymer particles
EP0628613B1 (en) Aqueous coating composition
JP3394588B2 (en) Aqueous coating composition
JPH0674369B2 (en) Method for producing aqueous dispersion of vinyl copolymer resin
JP2882730B2 (en) Aqueous coating composition
JP2859705B2 (en) Coating composition for paper polishing
JP2000319301A (en) Production of aqueous emulsion
JP2970765B2 (en) Primer for release paper using aqueous emulsion composition
JPH0827412A (en) Aqueous composition for coating film
JP2882733B2 (en) Aqueous coating composition
JP3807069B2 (en) Aqueous crosslinkable resin composition
JP3801762B2 (en) Water-based ink composition
JP3519119B2 (en) Aqueous coating composition and method for producing the same
JPH10176122A (en) Water-based coating composition
JP4050442B2 (en) Aqueous coating composition
JPH11286655A (en) Aqueous coating composition
JP2000027097A (en) Backside treating agent using aqueous emulsion for release paper
JP3421162B2 (en) Aqueous coating composition

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090205

Year of fee payment: 10

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100205

Year of fee payment: 11

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110205

Year of fee payment: 12

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110205

Year of fee payment: 12

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120205

Year of fee payment: 13

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120205

Year of fee payment: 13

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120205

Year of fee payment: 13

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120205

Year of fee payment: 13

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130205

Year of fee payment: 14

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130205

Year of fee payment: 14

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130205

Year of fee payment: 14

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130205

Year of fee payment: 14

EXPY Cancellation because of completion of term