JPH0798913B2 - Manufacturing method of resin for matte paint - Google Patents
Manufacturing method of resin for matte paintInfo
- Publication number
- JPH0798913B2 JPH0798913B2 JP21811489A JP21811489A JPH0798913B2 JP H0798913 B2 JPH0798913 B2 JP H0798913B2 JP 21811489 A JP21811489 A JP 21811489A JP 21811489 A JP21811489 A JP 21811489A JP H0798913 B2 JPH0798913 B2 JP H0798913B2
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- Prior art keywords
- meth
- weight
- acrylate
- polymerization
- resin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は特定の重合方法によって艶消し用の塗料樹脂を
製造する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing a paint resin for matting by a specific polymerization method.
[従来の技術] 艶消し塗料は、塗料に艶消し剤、例えば微粉末シリカ、
ポリエチレン微粉末などを添加してなり、塗膜表面にミ
クロな凹凸を発生せしめ、光の乱反射により低光沢にす
るものである。しかし、かかる処法においては艶消し剤
の悪影響が出やすく、例えば塗膜が摩擦されると、その
部分に艶が出て、外観がアンバランスになるなどの欠点
がある。[Prior Art] Matting paint is a matting agent such as fine powder silica,
It is made by adding polyethylene fine powder and the like to generate microscopic unevenness on the surface of the coating film, and lower the gloss by irregular reflection of light. However, in such a treatment method, the delusterant is liable to be adversely affected, and for example, when the coating film is rubbed, the portion is glossed and the appearance becomes unbalanced.
[発明が解決しようとする課題] 従って、かかる艶消し剤を用いなくても、実用的な艶消
し塗料が製造出来れば、その産業上の有用性は極めて大
であると言え、本発明は艶消し剤を配合せずして、実用
的な艶消し塗料を得ようとすることを目的とするもので
ある。[Problems to be Solved by the Invention] Therefore, it can be said that if a practical delustering paint can be produced without using such a delustering agent, its industrial usefulness will be extremely great. The purpose of the present invention is to obtain a practical matte paint without blending an eraser.
[課題を解決するための手段] 本発明においては、 (a)スチレン系化合物が10〜50重量% (b)アルキル基の炭素数が5以上の(メタ)アクリル
酸アルキルエステルが10〜30重量% (c)アルキル基の炭素数が1〜4の(メタ)アクリル
酸アルキルエステルが20〜80重量% の割合からなる樹脂の製造において、(a)と(b)と
の重合率が70〜90%に到達した時点で(c)を添加し
て、更に重合を進めることにより、前記の目的が達成出
来、艶消し塗料用樹脂として有用な樹脂が得られるので
ある。樹脂を構成する成分において(a)のスチレン系
化合物は10〜50重量%、好ましくは20〜40重量%であ
る。10重量%未満では艶消し効果が不充分であり、50重
量%を越える耐候性が乏しくなる。(b)のアルキル基
の炭素数が5以上の(メタ)アクリル酸アルキルは10〜
30重量%、好ましくは15〜25重量%である。10重量%以
下では艶消し効果が不充分となり、一方30重量%以上で
も艶消し効果が不充分となる。[Means for Solving the Problems] In the present invention, (a) a styrene compound is 10 to 50% by weight, and (b) an alkyl group (meth) acrylic acid alkyl ester having 5 or more carbon atoms is 10 to 30% by weight. % (C) In the production of a resin comprising 20 to 80% by weight of (meth) acrylic acid alkyl ester having 1 to 4 carbon atoms in the alkyl group, the polymerization rate of (a) and (b) is 70 to When 90% is reached, by adding (c) and further proceeding the polymerization, the above-mentioned object can be achieved and a resin useful as a resin for a matte coating can be obtained. In the component constituting the resin, the styrene compound (a) is 10 to 50% by weight, preferably 20 to 40% by weight. If it is less than 10% by weight, the matting effect is insufficient, and if it exceeds 50% by weight, the weather resistance becomes poor. Alkyl (meth) acrylate having 5 or more carbon atoms in the alkyl group (b) has 10 to
It is 30% by weight, preferably 15 to 25% by weight. If it is 10% by weight or less, the matte effect is insufficient, while if it is 30% by weight or more, the matte effect is insufficient.
(c)のアルキル基の炭素数が1〜4の(メタ)アクリ
ル酸アルキルエステルは20〜80重量%、好ましくは30〜
60重量%である。20重量%以下では艶消し効果が不充分
となり80重量%以上では樹脂溶液は層分離する。The (meth) acrylic acid alkyl ester having 1 to 4 carbon atoms in the alkyl group (c) is 20 to 80% by weight, preferably 30 to
60% by weight. If it is 20% by weight or less, the matte effect is insufficient, and if it is 80% by weight or more, the resin solution separates into layers.
本発明の樹脂を製造するに際しては通常有機溶剤を用い
た溶液重合が実施される。まず、所定量の(a)と
(b)とを有機溶剤に溶解し、ラジカル重合触媒を用い
て、(a)と(b)の重合を行う、(a)と(b)との
重合率が70〜90%に到達した時点で系に(c)を加え、
更に重合を進め、目的とする樹脂溶液を得る。In producing the resin of the present invention, solution polymerization using an organic solvent is usually carried out. First, a predetermined amount of (a) and (b) is dissolved in an organic solvent and the radical polymerization catalyst is used to polymerize (a) and (b). The polymerization rate of (a) and (b) (C) was added to the system when
The polymerization is further advanced to obtain the desired resin solution.
重合率は重合途中に樹脂溶液をサンプルリングし、その
サンプル中の加熱残分と理論加熱残分との百分比として
測定する。The polymerization rate is measured as a percentage of the heating residue and the theoretical heating residue in the sample by sampling the resin solution during the polymerization.
重合率が70%未満の時点で(c)を加え、更に重合を進
めた場合には、艶消し効果が不充分であり、90%を越え
た時点で(c)を加え、更に重合すると得られた樹脂溶
液は層分離するなどの欠点が顕著となり、好ましくな
い。When (c) is added when the polymerization rate is less than 70% and the polymerization is further advanced, the matting effect is insufficient, and when (c) is exceeded and 90% is exceeded, further polymerization is obtained. The resin solution thus obtained is not preferable because the defects such as layer separation become remarkable.
(a)のスチレン系化合物としては、スチレン、ビニル
トルエンなどが挙げられる。Examples of the styrene compound (a) include styrene and vinyltoluene.
(b)のアルキル基の炭素数が5以上の(メタ)アクリ
ル酸アルキルエステルとしては、(メタ)アクリル酸ア
ミル、(メタ)アクリル酸ヘキシル、(メタ)アクリル
酸ヘプチル、(メタ)アクリル酸オクチル、(メタ)ア
クリル酸2−エチルヘキシル、(メタ)アクリル酸デシ
ル、(メタ)アクリル酸ラウリル、(メタ)アクリル酸
ステアリルなどが挙げられ、単独又は2種以上併用され
る。その他のモノマーとして(メタ)アクリル酸2−ヒ
ドロキシエチル、(メタ)アクリル酸2−ヒドロキシプ
ロピルなどのヒドロキシ基含有(メタ)アクリル酸アル
キルも少量併用しうる。Examples of the (meth) acrylic acid alkyl ester in which the alkyl group of (b) has 5 or more carbon atoms include amyl (meth) acrylate, hexyl (meth) acrylate, heptyl (meth) acrylate, and octyl (meth) acrylate. , 2-ethylhexyl (meth) acrylate, decyl (meth) acrylate, lauryl (meth) acrylate, stearyl (meth) acrylate and the like can be used alone or in combination of two or more. As another monomer, a small amount of a hydroxy group-containing alkyl (meth) acrylate such as 2-hydroxyethyl (meth) acrylate or 2-hydroxypropyl (meth) acrylate may be used in combination.
(c)のアルキル基の炭素数1〜4の(メタ)アクリル
酸アルキルエステルとしては、(メタ)アクリル酸メチ
ル、(メタ)アクリル酸エチル、(メタ)アクリル酸プ
ロピル、(メタ)アクリル酸イソプロピル、(メタ)ア
クリル酸ブチル、(メタ)アクリル酸イソブチル、(メ
タ)アクリル酸sec−ブチル、(メタ)アクリル酸t−
ブチルなどが挙げられ、単独又は2種以上併用される。Examples of the (meth) acrylic acid alkyl ester having 1 to 4 carbon atoms of the alkyl group of (c) include methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate, and isopropyl (meth) acrylate. , Butyl (meth) acrylate, isobutyl (meth) acrylate, sec-butyl (meth) acrylate, t- (meth) acrylate
Butyl etc. are mentioned, and they are used individually or in combination of 2 or more types.
必要に応じてその他のモノマーとして(メタ)アクリル
酸2−ヒドロキシエチル、(メタ)アクリル酸2−ヒド
ロキシプロピルなどのヒドロキシル基含有(メタ)アク
リル酸アルキル、(メタ)アクリルアミドなどの重合性
アミド、酢酸ビニル、プロピオン酸ビニルなどのビニル
化合物、(メタ)アクリル酸、クロトン酸、イタコン
酸、(無水)マレイン酸、フマル酸などの不飽和カルボ
ン酸、ジメチルアミノエチルアクリレート、ジエチルア
ミノエチルメタクリレートなどの塩基性モノマーアルキ
ル基の炭素数が5以上の(メタ)アクリル酸アルキルエ
ステルも少量併用しうる。If necessary, as another monomer, a hydroxyl group-containing alkyl (meth) acrylate such as 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, a polymerizable amide such as (meth) acrylamide, acetic acid Vinyl, vinyl compounds such as vinyl propionate, unsaturated carboxylic acids such as (meth) acrylic acid, crotonic acid, itaconic acid, (anhydrous) maleic acid and fumaric acid, basic monomers such as dimethylaminoethyl acrylate and diethylaminoethyl methacrylate A small amount of (meth) acrylic acid alkyl ester having an alkyl group having 5 or more carbon atoms may be used together.
本発明の塗料用樹脂は、有機溶剤を用いた溶液重合法で
製造されるのが好ましいことは、前記した通りである
が、有機溶剤としてはトルエン、キシレンなどの芳香族
炭化水素、酢酸エチル、酢酸ブチルなどのエステル、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、イソプロピルアルコール、n−ブタノールなどの脂
肪族アルコール、エチレングリコールモノメチルエーテ
ル、エチレングリコールモノエチルエーテルなどが挙げ
られ、単独又は併用されるが、トルエン、キシレンなど
の芳香族炭化水素の単独又は併用が好ましい。The coating resin of the present invention is preferably produced by a solution polymerization method using an organic solvent, as described above, but as the organic solvent, toluene, an aromatic hydrocarbon such as xylene, ethyl acetate, Examples include esters such as butyl acetate, ketones such as methyl ethyl ketone and methyl isobutyl ketone, isopropyl alcohol, aliphatic alcohols such as n-butanol, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, and the like, which may be used alone or in combination. Aromatic hydrocarbons such as, and xylene are preferably used alone or in combination.
重合触媒としては、公知のラジカル重合触媒、例えばア
ゾビスイソブチロニトリル、ベンゾイルパーオキサイ
ド、ジーターシャリーブチルパーオキサイド、クメンハ
イドロパーオキサイドなどが用いられる。As the polymerization catalyst, known radical polymerization catalysts such as azobisisobutyronitrile, benzoyl peroxide, ditertiary butyl peroxide and cumene hydroperoxide are used.
重合時の温度は60〜150℃が適当であり、又重合時間は
6〜20時間程度が実用的である。A suitable temperature for the polymerization is 60 to 150 ° C., and a practical polymerization time is about 6 to 20 hours.
本発明の塗料用樹脂は前記の如く重合時に用いた有機溶
剤がそのまま溶剤となった状態で、塗料用樹脂として実
用に供せられるが、必要であれば、それを任意の溶剤に
置換して用いても差し支えない。The coating resin of the present invention can be put to practical use as a coating resin in a state where the organic solvent used during the polymerization is directly used as a solvent as described above, but if necessary, it may be replaced with any solvent. You can use it.
本発明の塗料用樹脂を使用して塗料を調製する時に使用
する顔料としては、酸化チタン、炭酸カルシウム、タル
ク、リトボン、硫酸バリウム、硫酸カルシウム、アルミ
ナ、クレーなどの白顔料、カーボンブラック、鉄黒など
の黒顔料、フタロシアニンブルー、紺青、群青などの青
顔料、レーキイエロー、黄鉛、オーカイエロー、ハンザ
イエローなどの黄顔料、ベンガラ、レーキレッドなどの
赤顔料、クロムバーミリオンなどの橙顔料、フタロシア
ニングリーン、酸化クロムなどの緑顔料などが挙げられ
る。Examples of pigments used when preparing coating materials using the coating resin of the present invention include titanium oxide, calcium carbonate, talc, lithobon, barium sulfate, calcium sulfate, alumina, white pigments such as clay, carbon black, iron black. Such as black pigments, phthalocyanine blue, navy blue, ultramarine blue pigments, lake yellow, yellow lead, oak yellow, hansa yellow, etc. yellow pigments, red iron oxide such as red iron oxide, lake red, chrome vermilion, etc., phthalocyanine Examples include green pigments and green pigments such as chromium oxide.
そのほか必要に応じて可塑剤、タレ防止剤、沈澱防止
剤、消泡剤などが適宜配合される。In addition, if necessary, a plasticizer, an anti-sagging agent, an anti-settling agent, an antifoaming agent and the like are appropriately added.
塗料の調製には通常使用されるサンドミル、ディスパ
ー、ボールミルなど使用される。得られた塗料の塗装方
法としては、コテ塗り、刷毛塗り、ローラー塗り、スプ
レー塗装などの方法が採用される。A sand mill, a disper, a ball mill and the like which are usually used are used for preparing the paint. As a coating method of the obtained coating material, a method such as iron coating, brush coating, roller coating, spray coating or the like is adopted.
この塗料は、コンクリート、モルタル建築物、瓦、サイ
デングボードなどの外装材の上塗り塗料として、更に建
築物の内装、床用の塗料として用いられると落ち着いた
仕上がり感の塗面が得られる。When this paint is used as a top coat paint for exterior materials such as concrete, mortar buildings, roof tiles and siding boards, and as a paint for interiors and floors of buildings, it gives a calm finish.
[作用] 本発明においては(a)、(b)、(c)の各成分を二
段階に分けて重合することにより、艶消し剤を使用しな
くても、実用的な艶消し塗料が製造出来る。[Operation] In the present invention, the components (a), (b), and (c) are polymerized in two stages to produce a practical matting paint without using a matting agent. I can.
[実施例] 次に実施例によって本発明を更に詳しく説明する。EXAMPLES Next, the present invention will be described in more detail by way of examples.
実施例1 攪拌機、温度計、コンデンサーの付いた4l容四つ口フラ
スコに、スチレン325部、アクリル酸2−エチルヘキシ
ル260部、トルエン320部、ベンゾイルパーオキサイド1.
5部を仕込み、温度90℃で重合を開始し、途中ベンゾイ
ルパーオキサイドを追加し、重合開始から6時間で重合
率が90%に到達したのでメタクリル酸メチル715部を徐
々に仕込んだ。更に4時間反応を継続した後、トルエン
を追加し冷却して、固形分濃度45%、粘度3500cps/25℃
の樹脂溶液(A−1)を得た。(A−1)の組成はスチ
レン25重量%、アクリル酸2−エチルヘキシル20重量
%、メタクリル酸メチル55重量%であった。Example 1 A 4-liter four-necked flask equipped with a stirrer, a thermometer, and a condenser, 325 parts of styrene, 260 parts of 2-ethylhexyl acrylate, 320 parts of toluene, and benzoyl peroxide 1.
5 parts were charged, the polymerization was started at a temperature of 90 ° C., benzoyl peroxide was added on the way, and the polymerization rate reached 90% within 6 hours from the start of the polymerization, so 715 parts of methyl methacrylate was gradually charged. After continuing the reaction for an additional 4 hours, add toluene and cool to a solid content concentration of 45% and a viscosity of 3500 cps / 25 ° C.
To obtain a resin solution (A-1). The composition of (A-1) was 25% by weight of styrene, 20% by weight of 2-ethylhexyl acrylate and 55% by weight of methyl methacrylate.
実施例2 実施例1と同一のフラスコにスチレン390部、アクリル
酸2−エチルヘキシル195部、トルエン320部、ベンゾイ
ルパーオキサイド1.5部を仕込み、温度90℃で重合を開
始し、途中ベンゾイルパーオキサイドを追加し、重合開
始から6時間で重合率が90%に到達した後、メタクリル
酸n−ブチル715部を徐々に仕込んだ。更に4時間反応
を継続した後、トルエンを追加し冷却して、固形分濃度
45%、粘度3000cps/25℃の樹脂溶液(A−2)を得た。
(A−2)の組成はスチレン30重量%、アクリル酸2−
エチルヘキシル15重量%、メタクリル酸n−ブチル55重
量%であった。Example 2 The same flask as in Example 1 was charged with 390 parts of styrene, 195 parts of 2-ethylhexyl acrylate, 320 parts of toluene, and 1.5 parts of benzoyl peroxide, polymerization was initiated at a temperature of 90 ° C., and benzoyl peroxide was added on the way. Then, after the polymerization rate reached 90% within 6 hours from the initiation of polymerization, 715 parts of n-butyl methacrylate was gradually charged. After continuing the reaction for another 4 hours, add toluene and cool to obtain a solid content concentration.
A resin solution (A-2) having 45% and a viscosity of 3000 cps / 25 ° C. was obtained.
The composition of (A-2) is 30% by weight of styrene and 2-acrylic acid.
It was 15% by weight of ethylhexyl and 55% by weight of n-butyl methacrylate.
実施例3 実施例1と同一のフラスコにスチレン260部、メタアク
リル酸ラウリル195部、トルエン320部、ベンゾイルパー
オキサイド1.5部を仕込み、温度90℃で重合を開始し、
途中ベンゾイルパーオキサイドを追加し、重合開始から
7時間で重合率が85%に到達した後、メタクリル酸メチ
ル845部を徐々に仕込んだ。更に4時間反応を継続した
後、トルエンを追加し冷却して、固形分濃度45%、粘度
4000cps/25℃の樹脂溶液(A−3)を得た。(A−3)
の組成はスチレン20重量%、メタクリル酸ラウリル30重
量%、メタクリル酸メチル65重量%であった。Example 3 The same flask as in Example 1 was charged with 260 parts of styrene, 195 parts of lauryl methacrylate, 320 parts of toluene, and 1.5 parts of benzoyl peroxide, and polymerization was started at a temperature of 90 ° C.
Benzoyl peroxide was added on the way, and after the polymerization rate reached 85% within 7 hours from the start of polymerization, 845 parts of methyl methacrylate was gradually charged. After continuing the reaction for another 4 hours, add toluene and cool to obtain a solid content concentration of 45% and a viscosity.
A resin solution (A-3) of 4000 cps / 25 ° C was obtained. (A-3)
The composition was 20% by weight of styrene, 30% by weight of lauryl methacrylate and 65% by weight of methyl methacrylate.
実施例4 実施例1と同一のフラスコにスチレン260部、アクリル
酸ラウリル390部、トルエン320部、ベンゾイルパーオキ
サイド1.5部を仕込み、温度90℃で重合を開始し、途中
ベンゾイルパーオキサイドを追加し、重合開始から6時
間で重合率が80%に到達した後、メタクリル酸エチル65
0部を徐々に仕込んだ。更に4時間反応を継続した後、
トルエンを追加し冷却して、固形分濃度45%、粘度3800
cps/25℃の樹脂溶液(A−4)を得た。(A−4)の組
成はスチレン20重量%、アクリル酸ラウリル30重量%、
メタアクリル酸エチル50重量%であった。Example 4 260 parts of styrene, 390 parts of lauryl acrylate, 320 parts of toluene, and 1.5 parts of benzoyl peroxide were charged in the same flask as in Example 1, polymerization was started at a temperature of 90 ° C., and benzoyl peroxide was added on the way. After the polymerization rate reached 80% within 6 hours from the start of polymerization, ethyl methacrylate 65
0 copies were gradually added. After continuing the reaction for another 4 hours,
Toluene is added and cooled, solid content concentration 45%, viscosity 3800
A resin solution (A-4) of cps / 25 ° C was obtained. The composition of (A-4) is 20% by weight of styrene, 30% by weight of lauryl acrylate,
It was 50% by weight of ethyl methacrylate.
対照例1 攪拌機、温度計、コンデンサーの付いた4l容四つ口フラ
スコにスチレン325部、アクリル酸2−エチルヘキシル2
60部、メタクリル酸メチル715部、トルエン520部、ベン
ゾイルパーオキサイド1.2部を仕込み、温度90℃で重合
を開始した。途中ベンゾイルパーオキサイドを追加し、
重合を継続し、9時間反応した後、トルエンを追加し冷
却して、固形分濃度45%、粘度3300cps/25℃の樹脂溶液
(B−1)を得た。(B−1)の組成は(A−1)と同
一であった。Comparative Example 1 325 parts of styrene, 2-ethylhexyl acrylate 2 in a 4 l four-necked flask equipped with a stirrer, a thermometer, and a condenser.
60 parts, 715 parts of methyl methacrylate, 520 parts of toluene and 1.2 parts of benzoyl peroxide were charged, and polymerization was started at a temperature of 90 ° C. Add benzoyl peroxide on the way,
After continuing the polymerization and reacting for 9 hours, toluene was additionally added and cooled to obtain a resin solution (B-1) having a solid content concentration of 45% and a viscosity of 3300 cps / 25 ° C. The composition of (B-1) was the same as that of (A-1).
対照例2 実施例1において(a)と(b)との重合率を65%に変
更した以外は同例と同一の方法を行って固形分濃度45重
量%の樹脂(B−2)を得た。Comparative Example 2 A resin (B-2) having a solid content concentration of 45% by weight was obtained by the same method as in Example 1 except that the polymerization rate of (a) and (b) was changed to 65%. It was
対照例3 実施例1において(a)と(b)との重合率を95%に変
更した以外は同例と同一の方法を行って固形分濃度45重
量%の樹脂(B−3)を得たが樹脂溶液は不安定で層分
離した。Comparative Example 3 A resin (B-3) having a solid content concentration of 45% by weight was obtained by the same method as in Example 1 except that the polymerization rate of (a) and (b) was changed to 95%. However, the resin solution was unstable and the layers were separated.
塗料の調製及び塗膜外観の測定 樹脂溶液30部に酸化チタン40部、ガラスビース100部を2
50ml容ガラスビンに入れ、ペイントコンディショナーに
て30分間振とう分散させた後、更に同一の樹脂溶液を60
部追加し、ペイントコンディショナーにて10分間振とう
させ白塗料を得た。Preparation of paint and measurement of coating appearance 30 parts of resin solution with 40 parts of titanium oxide and 100 parts of glass beads 2
Place in a 50 ml glass bottle, shake with a paint conditioner for 30 minutes to disperse, and then add the same resin solution to 60 ml.
Parts were added and shaken with a paint conditioner for 10 minutes to obtain a white paint.
対照例の樹脂溶液についても前記と同様にして白塗料を
得た。A white paint was obtained in the same manner as above for the resin solution of the control example.
得られた白塗料100部にトルエン/キシレン(=1/1)の
シンナー40部を加え希釈した後、バーコーター#50でブ
リキ板に塗布乾燥した後、光沢計で60度鏡面反射光沢を
測定したところ、白塗料(A−1)、(A−2)、(A
−3)、(A−4)の光沢はそれぞれ35、30、25、20で
あり白塗料(B−1)、(B−2)の光沢はそれぞれ7
5、60であった。To 100 parts of the white paint obtained, 40 parts of toluene / xylene (= 1/1) was added to dilute it, and then it was applied to a tin plate with a bar coater # 50 and dried, and then the specular gloss at 60 degrees was measured with a gloss meter. After that, white paints (A-1), (A-2), (A
-3) and (A-4) have a gloss of 35, 30, 25 and 20, respectively, and the white paints (B-1) and (B-2) have a gloss of 7 respectively.
It was 5, 60.
[効果] 本発明においては、特定の重合方法を採用することによ
って、艶消し剤を使用しなくても該樹脂単独で艶消し塗
料として有用な樹脂を製造し得る。[Effect] In the present invention, by adopting a specific polymerization method, a resin useful as a matting paint can be produced by using the resin alone without using a matting agent.
Claims (1)
酸アルキルエステルが10〜30重量% (c)アルキル基の炭素数が1〜4の(メタ)アクリル
酸アルキルエステルが20〜80重量% の割合からなる艶消し塗料用樹脂を製造するに当たり、
まず(a)と(b)を重合し、重合率が70〜90%となっ
た後(c)を更に重合させることを特徴とする艶消し塗
料用樹脂の製造法。(A) 10 to 50% by weight of a styrene compound (b) 10 to 30% by weight of (meth) acrylic acid alkyl ester having 5 or more carbon atoms in an alkyl group (c) Number of carbon atoms in an alkyl group In producing a resin for a matte coating containing 20 to 80% by weight of (meth) acrylic acid alkyl ester of 1 to 4,
A method for producing a resin for a matte coating, which comprises first polymerizing (a) and (b) and then further polymerizing (c) after the polymerization rate reaches 70 to 90%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21811489A JPH0798913B2 (en) | 1989-08-23 | 1989-08-23 | Manufacturing method of resin for matte paint |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21811489A JPH0798913B2 (en) | 1989-08-23 | 1989-08-23 | Manufacturing method of resin for matte paint |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0381371A JPH0381371A (en) | 1991-04-05 |
| JPH0798913B2 true JPH0798913B2 (en) | 1995-10-25 |
Family
ID=16714849
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21811489A Expired - Fee Related JPH0798913B2 (en) | 1989-08-23 | 1989-08-23 | Manufacturing method of resin for matte paint |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0798913B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2502047B2 (en) * | 1992-04-30 | 1996-05-29 | 日本合成化学工業株式会社 | Manufacturing method of resin for matte paint |
| WO1995001228A1 (en) * | 1993-07-01 | 1995-01-12 | Henkel Corporation | Copolymers useful as printing vehicles |
| JP2007125739A (en) * | 2005-11-01 | 2007-05-24 | Kobe Steel Ltd | Fiber reinforced resin pellet and its manufacturing method |
| JP6847040B2 (en) * | 2015-09-07 | 2021-03-24 | 綜研化学株式会社 | Method for Producing (Meta) Acrylic Polymer and Method for Producing Adhesive Layer |
-
1989
- 1989-08-23 JP JP21811489A patent/JPH0798913B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0381371A (en) | 1991-04-05 |
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