JPH0573137B2 - - Google Patents
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- JPH0573137B2 JPH0573137B2 JP62275850A JP27585087A JPH0573137B2 JP H0573137 B2 JPH0573137 B2 JP H0573137B2 JP 62275850 A JP62275850 A JP 62275850A JP 27585087 A JP27585087 A JP 27585087A JP H0573137 B2 JPH0573137 B2 JP H0573137B2
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Description
(産業上の利用分野)
本発明は無機多孔質基材用シーラーに関し、更
に詳しくは、密着性、耐水性、耐久性、上塗り適
性等の諸特性に優れた無機多孔質基材用シーラー
に関する。
(従来の技術及び発明が解決しようとする問題
点)
無機多孔質基材のシーラに使用する樹脂として
は、従来より比較的低分子量の湿気硬化型ウレタ
ン樹脂や溶剤型樹脂等が用いられてきた。しかし
ながら前者はその毒性が、また後者は有機溶剤の
使用による火災の危険性や環境汚染等が問題にな
つており、水性化の要望が強くなつている。水系
シーラーとしては、水溶性樹脂や水分散性樹脂を
主成分とするものが種々検討されているが、水溶
性樹脂を主成分とするものは耐水性が、又、水分
散性樹脂を主成分とするものは基材への含浸性や
密着性が悪く、長期の耐久性を有していない。更
に水溶性樹脂と水性樹脂分散体を混合して用いる
方法が検討されており、例えばアクリルエマルシ
ヨンに5〜80%の水溶性樹脂をブレンドする方法
(特開昭61−141769)、特定の重合体水性エマルシ
ヨンにポリビニルアルコールをブレンドする方法
(特開昭53−97018)等が提案されているが、いず
れの方法も各々欠点が残され、十分な性能を有す
る水系シーラーは得られていないのが現状であ
る。
(問題点を解決するための技術的手段)
本発明は上記のような問題点即ち、湿気硬化型
ウレタンや溶剤系樹脂を主成分とするシーラーが
有する毒性、火災の危険性、環境汚染の問題や水
系シーラーが有する耐水性、含浸不足、密着性不
足、耐久性等の問題を一挙に解決したものであ
る。
本発明者らは鋭意研究の結果、アクリル系水性
樹脂分散物と特定のポリビニルアルコールとを重
合開始剤の存在下に特定条件で加熱処理して得ら
れる水性樹脂分散体は、従来の水系シーラーにみ
られる欠点が全く見られず、しかも毒性や環境汚
染等の心配も全く無いことを見出し、本発明を完
成するに至つた。
即ち、本発明は、アクリル系水性樹脂分散物、
鹸化度80オル%以上のポリビニルアルコールおよ
び重合開始剤からなる混合物を、40℃以上の温度
で加熱処理して得られる水性樹脂分散体を含有し
てなる無機多孔質基材用シーラーに関するもので
ある。
本発明におけるアクリル系水性樹脂分散物とし
ては、アクリル樹脂エマルシヨンの他、アクリル
−スチレン樹脂エマルシヨン、アクリル−酢酸ビ
ニルエマルシヨン、アクリル−スチレン−酢酸ビ
ニルエマルシヨン等のアクリル系共重合エマルシ
ヨンを挙げることができる。このようなアクリル
系水性樹脂分散物はアクリル系重合性単量体また
はこれと他の共重合性単量体を周知の方法で乳化
重合して得られるものであり、使用できる重合性
単量体としては、例えばメチル(メタ)アクリレ
ート、エチル(メタ)アクリレート、ブチル(メ
タ)アクリレート、2−エチルヘキシル(メタ)
アクリレート、シクロヘキシル(メタ)アクリレ
ートなどの(メタ)アクリレート類;(メタ)ア
クリロニトリルなどのアクリル系シアン化合物
類;ヒドロキシエチル(メタ)アクリレート、ヒ
ドロキシプロピル(メタ)アクリレートなどのヒ
ドロキシ基含有アクリル系単量体類;(メタ)ア
クリルアミド、N−メチロール(メタ)アクリル
アミドなどのアクリル系アミドまたはその誘導体
類;ジメチルアミノエチル(メタ)アクリレート
などのアミノ基含有アクリル系単量体類;エチレ
ングリコールジ(メタ)アクリレートなどの多官
能性アクリル系単量体類;グリシジル(メタ)ア
クリレート、アリルグリシジルエーテルなどのグ
リシジル基含有アクリル系単量体類;(メタ)ア
クリル酸、クロトン酸、イタコン酸、フマル酸、
マレイン酸、モノメチルフマレート及びモノエチ
ルマレートなどのアクリル系不飽和カルボン酸類
又はその誘導体などを挙げることができ、これら
の1種又は2種以上を使用することができる。
また、これらアクリル系単量体と共に、スチレ
ン、α−メチルスチレン、α−クロルスチレン、
ビニルトルエン等の芳香族不飽和単量体;フツ化
ビニル、塩化ビニルなどのハロゲン化ビニル、酢
酸ビニル、プロピオン酸ビニルなどのビニルエス
テル類等の共重合性単量体を併用することもでき
る。
本発明におけるアクリル系水性樹脂分散物は前
記重合性単量体を乳化剤の存在下又は不存在下に
重合開始剤を用いて乳化重合すればよく、重合開
始剤としては、例えば過硫酸アンモニウム、過硫
酸カリウム、過酸化水素、ベンゾイルパーオキサ
イド等の公知の水溶性もしくは油溶性開始剤を用
いることができる。また、この時還元剤として亜
硫酸水素ナトリウム、L−アスコルビン酸等を用
いてレドツクス系開始剤としてもよい。又、必要
により用いる乳化剤としてはラウリル硫酸ナトリ
ウム等のアニオン系活性剤、ポリオキシエチレン
アルキルエーテル等のノニオン系活性剤が挙げら
れる。更に、重合時に分子量調節を目的としてラ
ウリルメルカプタンのような連鎖移動剤を使用し
てもよい。また乳化重合時に重合性単量体等の組
成を各段階で変更して多段乳化重合を行なつても
よい。
本発明で用いるポリビニルアルコールは鹸化度
80モル%以上、好ましくは鹸化度87モル%以上の
ものである。鹸化度が80モル%未満のポリビニル
アルコールを用いると、結晶化度が低下したり親
水性が強くなり、無機多孔質基材用シーラーとし
て用いた場合の耐水性が低下するため好ましくな
い。本発明において用いるポリビニルアルコール
の使用量は特に限定されないが、無機多孔質基材
用シーラーとして用いる場合の該基材に対する密
着性や耐水性の面で水性樹脂分散物100重量部に
対して固形分比で1〜30重量部の範囲とするのが
好ましく、より好ましくは5〜25重量部とするの
が好適である。また本発明におけるポリビニルア
ルコールの重合度は最終的に得られる水性樹脂分
散体の耐水性や粘度の面で200〜2600の範囲とす
るのが好ましく、より好ましくは500〜2400の範
囲が好適である。尚、本発明に使用するポリビニ
ルアルコールとしては、ビニルアルコール単位の
一部が他のビニルモノマー単位で置換された重合
体又はポリビニルアルコール中に存在する水酸基
の水素の一部が他の化合物にて置換された重合
体、例えば一部ブチラール化等を行つた重合体で
あつても構わない。
本発明の水性樹脂分散体を製造する際に用いる
重合開始剤としては、前記水性樹脂分散物の乳化
重合に用いたものがそのまま用いられる。また、
必要により前記還元剤を用いてもよい。このとき
用いられる重合開始剤の量は、前記アクリル系水
性樹脂分散物とポリビニルアルコールの総固形分
に対して0.02〜0.2重量%(ポリビニルアルコー
ルの固形分換算で0.01〜0.1重量%)とするのが
よく、0.02重量%未満ではその添加効果が有効に
発現せず、一方0.2重量%を超えると、加熱処理
工程で粘性が過度に高まり、無機多孔質基材用シ
ーラーとしての適性が失なわれる。
本発明の無機多孔質基材用シーラーは前記アク
リル性樹脂分散物、鹸化度80モル%以上のポリビ
ニルアルコール及び重合開始剤からなる混合物を
40度以上の温度、好ましくは50〜95℃の温度で加
熱処理して得られるものである。本発明において
上記混合物を加熱処理する意義は、アクリル系水
性樹脂分散物とポリビニルアルコールとの単なる
混合物に比べて、無機多孔質基材に塗装した場合
に、基材への含浸性が低下することなく密着性や
耐水性が向上すると共に、ポリビニルアルコール
の使用量も低減できることにある。加熱処理の温
度が40℃未満では、重合開始剤の分解が極めて遅
くなると共にポリビニルアルコールの水に対する
溶解性が低下し、加熱処理効果が有効に発揮され
なくなつて上記特徴を有する無機多孔質基材用シ
ーラーが得られない。
本発明の無機多孔質基材用シーラーは、上記手
順により得られるアクリル系水性樹脂分散体を含
んでなるものである。この水性樹脂分散体はその
まま本発明の無機多孔質基材用シーラーとして使
用できるが、必要に応じて成膜助剤、顔料、充填
剤、トナー、湿潤剤等を配合して用いても良い。
但し、顔料、充填剤およびトナーの使用量は、上
記アクリル系水性樹脂分散体の特徴を損なわない
ため、水性樹脂分散体100重量部(不揮発分換算)
当り300重量部以下とするのが好ましい。
(発明の効果)
本発明の無機多孔質基材用シーラーは、前述の
如くアクリル系水性樹脂分散体、ポリビニルアル
コールおよび重合開始剤からなる混合物を加熱処
理することによつて得られる水性樹脂分散物を有
効成分として含有するものであり、耐凍害性等の
耐久性、上塗り塗料の塗装時の耐リフテイング
性、上塗り塗膜との層間密着性のいずれにおいて
も優れたものであり、該水例えばモルタル、コン
クリート、軽量気泡コンクリート、スレート板、
珪酸カルシウム板等の基材へのシーラーに好適に
用いることができる。
(実施例)
以下実施例によつて本発明を詳細に説明する
が、本発明は以下の実施例によつて限定されるも
のではない。なお、例中の部は特にことわりが無
い限り重量による。
製造例 1
攪拌器、還流冷却器、滴下ロート、温度計を備
えた1のセパラブルフラスコに脱イオン水500
部、ラウリル硫酸ナトリウム8部を仕込んだ後、
窒素ガスを吹き込みながら、攪拌下に70℃まで昇
温した。しかる後、メタクリル酸メチル160部、
スチレン80部、ブチルアクリレート152部、メタ
クリル酸8部からなる重合性単量体混合物を2時
間にわたつて均一に滴下した。この間同時に10%
の過硫酸アンモニウム水溶液10部を2時間にわた
つて均一に滴下した。その後1時間熟成を行つた
後、冷却した。こうして得た水性樹脂分散物(1)は
不揮発分43.5%、PH9.0、粘度150cps(B型粘度
計)、最低成膜温度35℃の特数値を示した。得ら
れた水性樹脂分散物(1)200部とクラレポバール
PVA−117(クラレ(株)製ポリビニルアルコール:
重合度1700、鹸化度98〜99モル%)の10%水溶液
150部をセパラブルフラスコに仕込んだ後、窒素
ガスを吹き込みながら、攪拌下に70℃まで昇温し
た。しかる後、過硫酸アンモニウムの1%水溶液
2部を添加して60分間70℃で加熱処理を行つた。
加熱処理終了後、直ちに冷却を行い、25%のアン
モニア水を6.3部添加して水性樹脂分散体(1)を得
た。得られた水性樹脂分散体(1)は不揮発分29.0
%、PH8.9、粘度3000cps(B型粘度計)最低成膜
温度0℃以下の特数値を示した。得られた水性樹
脂分散体(1)をテフロン板上に塗布して乾燥した
後、剥離して得られた塗膜を水を溶媒としてソツ
クスレー抽出器を用いて、沸点で4時間加熱して
ポリビニルアルコールを塗膜より抽出したところ
塗膜100部に対して0.2部のポリビニルアルコール
の抽出が確認できた。
製造例 2
製造例1で用いたのと同じセパラブルフラスコ
に脱イオン水350部を仕込んだ後、窒素ガスを吹
き込みながら、攪拌下に60℃まで昇温した。しか
る後、メチルメタクリレート200部、シクロヘキ
シルメタクリレート100部、2−エチルヘキシル
アクリレート90部、グリシジルメタクリレート4
部、アクリル酸6部からなる重合性単量体混合物
にエマルゲン950(花王(株)製:ポリオキシエチレン
ノニルフエニルエーテル)10部、レベノールWZ
(花王(株)製:ポリオキシエチレンノニルフエニル
エーテル硫酸ナトリウムの25%水溶液)16部、脱
イオン水120部を加えてなるプレエマルシヨン混
合物を3時間にわたつて均一に滴下を行つた。こ
の間2%の過硫酸カリウム水溶液60部と5%の亜
硫酸水素ナトリウム水溶液12部を10分毎にプレエ
マルシヨン混合物の滴下終了まで分割してフラス
コに添加した。滴下終了後、1時間熟成を行い冷
却した。こうして得た水性樹脂分散物(2)は不揮発
分42.5%、PH9.1、粘度84cps(B型粘度計)、最低
成膜温度65℃の特数値を示した。得られた水性樹
脂分散物(2)200部とクラレポバールPVA−205(ク
ラレ(株)製 ポリビニルアルコール:重合度500、
鹸化度87〜89モル%)の10%水溶液290部をセパ
ラブルフラスコに仕込んだ後、窒素ガスを吹き込
みながら、攪拌下に50℃まで昇温した。しかる
後、過酸化水素の2%水溶液14.5部と5%L−ア
スコルビン酸水溶液3部を添加して2時間加熱処
理を行つた後、冷却して、25%のアンモニア水を
5.7部添加し、中和を行つた。こうして得られた
水性樹脂分散体(2)は不揮発分24.5%、PH8.9、粘
度45cps(B型粘度計)、最低成膜温度23℃の特数
値を示した。得られた水性樹脂分散体(2)をテフロ
ン板上に塗布した後、剥離して得られた塗膜を製
造例1と同様の方法でポリビニルアルコールの抽
出を行つたところ、塗膜100部に対して0.5部のポ
リビニルアルコールの抽出が確認できた。
製造例 3
製造例1で得られた水性樹脂分散物(1)を重合終
了直後に85℃まで昇温した後、水性樹脂分散物(1)
200部当たり5%のクラレポバールPVA−124(ク
ラレ(株)製 ポリビニルアルコール:重合度2400、
鹸化度98〜99モル%)100部を添加し、更に2%
の過硫酸カリウム水溶液1部を添加して、30分間
加熱処理を行つた後、冷却して、25%のアンモニ
ア水を6.3部添加して中和を行い、水性樹脂分散
体(3)を得た。得られた水性樹脂分散体(3)は不揮発
分30.0%、PH9.0、粘度220cps(B型粘度計)、最
低成膜温度13℃の特数値を示した。得られた水性
樹脂分散体(3)をテフロン板上に塗布して得られた
塗膜を製造例1と同様の方法でポリビニルアルコ
ールの抽出を行つたところ、塗膜100部当たり0.1
部のポリビニルアルコールの抽出が確認できた。
比較製造例 1
製造例1で得られた水性樹脂分散物(1)200部に
25%のアンモニア水を6.3部添加した後、クラレ
ポバールPVA−117の10%水溶液150部を混合し
て比較用水性樹脂分散体(1)を得た。この比較用水
性樹脂分散体(1)は不揮発分29.0%、PH8.9、粘度
2200cps(B型粘度計)、最低成膜温度0℃以下の
特数値を示した。この比較用水性樹脂分散体(1)を
テフロン板上に塗布して得られた塗膜を製造例1
と同様の方法でポリビニルアルコールの抽出を行
つたところ、塗膜100部当たり12.7部のポリビニ
ルアルコールの抽出が確認できた。
比較製造例 2
製造例2で得られた水性樹脂分散物(2)200部に
25%のアンモニア水を5.7部添加した後、クラレ
ポバールPVA−205の10%水溶液290部を添加し
てよく混合し、比較用水性樹脂分散体(2)を得た。
この比較用水性樹脂分散体(2)は不揮発分24.6%、
PH9.2、粘度36cps(B型粘度計)、最低成膜温度45
℃を示した。この比較用水性樹脂分散体(2)をテフ
ロン板上に塗布して得られた塗膜を製造例1と同
様の方法でポリビニルアルコールの抽出を行つた
ところ、塗膜100部当たり、23.4部のポリビニル
アルコールの抽出が確認できた。
比較製造例 3
攪拌器、還流冷却器、温度計を備えた1のセ
パラブルフラスコにクラレポバールPVA−117の
10%水溶液600部を仕込んだ後、窒素ガスを吹き
込みながら、攪拌下に70℃まで昇温した。しかる
後、過硫酸アンモニウムの1%水溶液8部を添加
して、70℃で60分間加熱処理を行つた。得られた
加熱処理済のPVA−117水溶液152部を製造例1
で得られた水性樹脂分散物(1)200部に加えた後、
よく混合し、更に25%のアンモニア水を6.3部添
加して比較用水性樹脂分散体(3)を得た。この比較
用水性樹脂分散体(3)は不揮発分28.9%、PH8.8、
粘度2080cps(B型粘度計)、最低成膜温度0℃以
下の特数値を示した。この比較用水性樹脂分散体
(3)をテフロン板上に塗布して得られた塗膜を製造
例1と同様の方法でポリビニルアルコールの抽出
を行つたところ、塗膜100部当たり10.9部の抽出
が確認できた。
製造例 1
製造例1〜3で得られた水性樹脂分散体(1)〜(3)
および比較製造例1〜3で得られた比較用水性樹
脂分散体(1)〜(3)を用い、水性樹脂分散体(1)、(3)お
よび比較用水性樹脂分散体(1)〜(3)はそのまま、水
性樹脂分散体(2)は該分散体(2)100部に対してCS−
12(チツソ(株)製の成膜助剤)を2部添加してそれ
ぞれ無機多孔質基材用シーラー(1)〜(3)および比較
用無機多孔質基材用シーラー(1)〜(3)とし、これら
を第1表に示した無機多孔質基材上に20g/m2塗
布し、120℃で10分間熱風乾燥器中で乾燥した後、
塗膜の基材に対する密着性、耐温水性及び耐凍害
性を調べた。結果は第1表に示したとおりであつ
た。
(Field of Industrial Application) The present invention relates to a sealer for inorganic porous substrates, and more particularly to a sealer for inorganic porous substrates that has excellent properties such as adhesion, water resistance, durability, and suitability for overcoating. (Prior art and problems to be solved by the invention) Conventionally, relatively low molecular weight moisture-curing urethane resins, solvent-based resins, etc. have been used as resins for sealing inorganic porous substrates. . However, the former poses problems due to its toxicity, and the latter poses problems such as fire danger and environmental pollution due to the use of organic solvents, and there is a strong demand for water-based compositions. Various types of water-based sealers that have water-soluble resins or water-dispersible resins as their main ingredients have been studied. Those that have such properties have poor impregnating properties and adhesion to substrates, and do not have long-term durability. Furthermore, methods using a mixture of a water-soluble resin and an aqueous resin dispersion are being considered, such as a method of blending 5 to 80% of a water-soluble resin into an acrylic emulsion (Japanese Patent Application Laid-Open No. 141769/1989), Methods such as blending polyvinyl alcohol into a combined aqueous emulsion (Japanese Patent Application Laid-Open No. 53-97018) have been proposed, but each method has its own drawbacks, and a water-based sealer with sufficient performance has not been obtained. This is the current situation. (Technical means for solving the problems) The present invention solves the above-mentioned problems, namely, the toxicity, fire danger, and environmental pollution of sealers whose main components are moisture-curing urethane and solvent-based resins. This solution solves all the problems of water-based sealers such as water resistance, insufficient impregnation, insufficient adhesion, and durability. As a result of extensive research, the present inventors have found that an aqueous resin dispersion obtained by heat-treating an acrylic aqueous resin dispersion and a specific polyvinyl alcohol under specific conditions in the presence of a polymerization initiator can be used as a conventional aqueous sealer. The present inventors have discovered that they do not have any of the above-mentioned drawbacks, and that there is no fear of toxicity or environmental pollution, leading to the completion of the present invention. That is, the present invention provides an acrylic aqueous resin dispersion,
This relates to a sealer for inorganic porous substrates containing an aqueous resin dispersion obtained by heat-treating a mixture of polyvinyl alcohol with a saponification degree of 80 ol% or higher and a polymerization initiator at a temperature of 40°C or higher. . Examples of the acrylic aqueous resin dispersion in the present invention include acrylic resin emulsions as well as acrylic copolymer emulsions such as acrylic-styrene resin emulsions, acrylic-vinyl acetate emulsions, and acrylic-styrene-vinyl acetate emulsions. can. Such an acrylic aqueous resin dispersion is obtained by emulsion polymerization of an acrylic polymerizable monomer or this and other copolymerizable monomers by a well-known method. For example, methyl (meth)acrylate, ethyl (meth)acrylate, butyl (meth)acrylate, 2-ethylhexyl (meth)
(Meth)acrylates such as acrylate and cyclohexyl (meth)acrylate; Acrylic cyanide compounds such as (meth)acrylonitrile; Hydroxy group-containing acrylic monomers such as hydroxyethyl (meth)acrylate and hydroxypropyl (meth)acrylate Acrylic amides or derivatives thereof such as (meth)acrylamide and N-methylol (meth)acrylamide; Amino group-containing acrylic monomers such as dimethylaminoethyl (meth)acrylate; Ethylene glycol di(meth)acrylate Polyfunctional acrylic monomers such as; glycidyl group-containing acrylic monomers such as glycidyl (meth)acrylate and allyl glycidyl ether; (meth)acrylic acid, crotonic acid, itaconic acid, fumaric acid,
Examples include acrylic unsaturated carboxylic acids such as maleic acid, monomethyl fumarate, and monoethyl maleate, or derivatives thereof, and one or more of these may be used. In addition to these acrylic monomers, styrene, α-methylstyrene, α-chlorostyrene,
Aromatic unsaturated monomers such as vinyl toluene; copolymerizable monomers such as vinyl halides such as vinyl fluoride and vinyl chloride; and vinyl esters such as vinyl acetate and vinyl propionate can also be used in combination. The aqueous acrylic resin dispersion of the present invention may be prepared by emulsion polymerizing the polymerizable monomers using a polymerization initiator in the presence or absence of an emulsifier. Examples of the polymerization initiator include ammonium persulfate, persulfate Known water-soluble or oil-soluble initiators such as potassium, hydrogen peroxide, and benzoyl peroxide can be used. Further, at this time, sodium bisulfite, L-ascorbic acid, etc. may be used as a reducing agent to form a redox-based initiator. Examples of emulsifiers used as necessary include anionic activators such as sodium lauryl sulfate and nonionic activators such as polyoxyethylene alkyl ether. Furthermore, a chain transfer agent such as lauryl mercaptan may be used for the purpose of controlling the molecular weight during polymerization. Furthermore, multi-stage emulsion polymerization may be performed by changing the composition of polymerizable monomers and the like at each stage during emulsion polymerization. The polyvinyl alcohol used in the present invention has a saponification degree of
The degree of saponification is 80 mol% or more, preferably 87 mol% or more. Use of polyvinyl alcohol with a saponification degree of less than 80 mol % is not preferred because the degree of crystallinity decreases or the hydrophilicity becomes strong, resulting in a decrease in water resistance when used as a sealer for inorganic porous substrates. The amount of polyvinyl alcohol used in the present invention is not particularly limited, but when used as a sealer for inorganic porous substrates, the solid content is determined based on 100 parts by weight of the aqueous resin dispersion in terms of adhesion to the substrate and water resistance. The ratio is preferably in the range of 1 to 30 parts by weight, more preferably 5 to 25 parts by weight. Further, the degree of polymerization of the polyvinyl alcohol in the present invention is preferably in the range of 200 to 2,600, more preferably in the range of 500 to 2,400 in terms of water resistance and viscosity of the aqueous resin dispersion finally obtained. . The polyvinyl alcohol used in the present invention is a polymer in which a portion of the vinyl alcohol units are substituted with other vinyl monomer units, or a polymer in which a portion of the hydrogen atoms of the hydroxyl groups present in the polyvinyl alcohol are substituted with other compounds. For example, a partially butyralized polymer may be used. As the polymerization initiator used in producing the aqueous resin dispersion of the present invention, those used in the emulsion polymerization of the aqueous resin dispersion described above can be used as they are. Also,
The above-mentioned reducing agent may be used if necessary. The amount of the polymerization initiator used at this time is 0.02 to 0.2% by weight based on the total solid content of the aqueous acrylic resin dispersion and polyvinyl alcohol (0.01 to 0.1% by weight in terms of solid content of polyvinyl alcohol). If it is less than 0.02% by weight, the effect of its addition will not be effectively expressed, while if it exceeds 0.2% by weight, the viscosity will increase excessively during the heat treatment process, and the suitability as a sealer for inorganic porous substrates will be lost. . The sealer for inorganic porous substrates of the present invention contains a mixture consisting of the acrylic resin dispersion, polyvinyl alcohol with a saponification degree of 80 mol% or more, and a polymerization initiator.
It is obtained by heat treatment at a temperature of 40 degrees Celsius or higher, preferably at a temperature of 50 to 95 degrees Celsius. In the present invention, the significance of heat-treating the above mixture is that, compared to a simple mixture of an acrylic aqueous resin dispersion and polyvinyl alcohol, when applied to an inorganic porous substrate, the impregnation into the substrate is reduced. In addition to improving adhesion and water resistance, the amount of polyvinyl alcohol used can also be reduced. If the heat treatment temperature is less than 40°C, the decomposition of the polymerization initiator will be extremely slow, and the solubility of polyvinyl alcohol in water will decrease, and the heat treatment effect will not be effectively exerted, resulting in an inorganic porous group having the above characteristics. I can't get a sealer for wood. The sealer for inorganic porous substrates of the present invention contains the aqueous acrylic resin dispersion obtained by the above procedure. This aqueous resin dispersion can be used as it is as the sealer for inorganic porous substrates of the present invention, but if necessary, it may be used by adding film-forming aids, pigments, fillers, toners, wetting agents, etc.
However, the amount of pigment, filler, and toner used is 100 parts by weight of the aqueous resin dispersion (in terms of non-volatile content) in order not to impair the characteristics of the above-mentioned acrylic aqueous resin dispersion.
The amount is preferably 300 parts by weight or less. (Effects of the Invention) The sealer for inorganic porous substrates of the present invention is an aqueous resin dispersion obtained by heat-treating a mixture consisting of an acrylic aqueous resin dispersion, polyvinyl alcohol, and a polymerization initiator, as described above. It contains as an active ingredient, and is excellent in terms of durability such as frost damage resistance, lifting resistance during the application of the top coat, and interlayer adhesion with the top coat. , concrete, lightweight aerated concrete, slate board,
It can be suitably used as a sealer for base materials such as calcium silicate plates. (Examples) The present invention will be described in detail below with reference to Examples, but the present invention is not limited to the following Examples. In addition, parts in the examples are by weight unless otherwise specified. Production example 1 500ml of deionized water was added to a separable flask equipped with a stirrer, reflux condenser, dropping funnel, and thermometer.
After adding 8 parts of sodium lauryl sulfate,
The temperature was raised to 70° C. while stirring and blowing nitrogen gas. After that, 160 parts of methyl methacrylate,
A polymerizable monomer mixture consisting of 80 parts of styrene, 152 parts of butyl acrylate, and 8 parts of methacrylic acid was uniformly dropped over 2 hours. 10% at the same time during this period
10 parts of an aqueous ammonium persulfate solution was uniformly added dropwise over 2 hours. Thereafter, the mixture was aged for 1 hour and then cooled. The thus obtained aqueous resin dispersion (1) exhibited the following special values: non-volatile content of 43.5%, pH of 9.0, viscosity of 150 cps (B-type viscometer), and minimum film forming temperature of 35°C. 200 parts of the obtained aqueous resin dispersion (1) and Kuraray Poval
PVA-117 (Polyvinyl alcohol manufactured by Kuraray Co., Ltd.:
10% aqueous solution with polymerization degree of 1700 and saponification degree of 98-99 mol%)
After charging 150 parts into a separable flask, the temperature was raised to 70° C. while stirring while blowing nitrogen gas. Thereafter, 2 parts of a 1% aqueous solution of ammonium persulfate was added, and heat treatment was performed at 70°C for 60 minutes.
Immediately after the heat treatment was completed, it was cooled and 6.3 parts of 25% ammonia water was added to obtain an aqueous resin dispersion (1). The obtained aqueous resin dispersion (1) has a nonvolatile content of 29.0
%, PH8.9, viscosity 3000 cps (B-type viscometer), and the minimum film forming temperature was 0°C or less. The resulting aqueous resin dispersion (1) was coated on a Teflon plate and dried, then peeled off and the resulting coating film was heated at boiling point for 4 hours using a Soxhlet extractor with water as a solvent to obtain polyvinyl When alcohol was extracted from the paint film, it was confirmed that 0.2 parts of polyvinyl alcohol was extracted per 100 parts of the paint film. Production Example 2 After 350 parts of deionized water was charged into the same separable flask as used in Production Example 1, the temperature was raised to 60° C. while stirring while blowing nitrogen gas. After that, 200 parts of methyl methacrylate, 100 parts of cyclohexyl methacrylate, 90 parts of 2-ethylhexyl acrylate, 4 parts of glycidyl methacrylate
10 parts of Emulgen 950 (manufactured by Kao Corporation: polyoxyethylene nonyl phenyl ether) and Lebenol WZ to a polymerizable monomer mixture consisting of 6 parts of acrylic acid and 6 parts of acrylic acid.
A pre-emulsion mixture prepared by adding 16 parts of a 25% aqueous solution of sodium polyoxyethylene nonyl phenyl ether sulfate (manufactured by Kao Corporation) and 120 parts of deionized water was uniformly dropped over a period of 3 hours. During this time, 60 parts of a 2% aqueous potassium persulfate solution and 12 parts of a 5% aqueous sodium bisulfite solution were added to the flask in portions every 10 minutes until the dropwise addition of the pre-emulsion mixture was completed. After the dropwise addition was completed, the mixture was aged for 1 hour and cooled. The thus obtained aqueous resin dispersion (2) exhibited the following special values: nonvolatile content of 42.5%, pH of 9.1, viscosity of 84 cps (B-type viscometer), and minimum film-forming temperature of 65°C. 200 parts of the obtained aqueous resin dispersion (2) and Kuraray Poval PVA-205 (manufactured by Kuraray Co., Ltd. Polyvinyl alcohol: degree of polymerization 500,
After charging 290 parts of a 10% aqueous solution with a degree of saponification of 87 to 89 mol%) into a separable flask, the temperature was raised to 50° C. with stirring while blowing nitrogen gas. Thereafter, 14.5 parts of a 2% aqueous solution of hydrogen peroxide and 3 parts of a 5% aqueous L-ascorbic acid solution were added, heat treated for 2 hours, cooled, and 25% aqueous ammonia was added.
5.7 parts were added to perform neutralization. The thus obtained aqueous resin dispersion (2) exhibited the following special values: non-volatile content of 24.5%, pH of 8.9, viscosity of 45 cps (B-type viscometer), and minimum film-forming temperature of 23°C. After coating the obtained aqueous resin dispersion (2) on a Teflon plate and peeling it off, polyvinyl alcohol was extracted from the resulting coating film in the same manner as in Production Example 1. It was confirmed that 0.5 part of polyvinyl alcohol was extracted. Production Example 3 After heating the aqueous resin dispersion (1) obtained in Production Example 1 to 85°C immediately after the completion of polymerization, the aqueous resin dispersion (1)
5% per 200 parts of Kuraray Poval PVA-124 (manufactured by Kuraray Co., Ltd. Polyvinyl alcohol: degree of polymerization 2400,
Saponification degree 98-99 mol%) was added to 100 parts, and then 2%
After adding 1 part of potassium persulfate aqueous solution and heating for 30 minutes, it was cooled and neutralized by adding 6.3 parts of 25% aqueous ammonia to obtain an aqueous resin dispersion (3). Ta. The obtained aqueous resin dispersion (3) exhibited special values of non-volatile content of 30.0%, pH of 9.0, viscosity of 220 cps (B type viscometer), and minimum film forming temperature of 13°C. The obtained aqueous resin dispersion (3) was applied on a Teflon plate, and polyvinyl alcohol was extracted from the resulting coating film in the same manner as in Production Example 1. As a result, polyvinyl alcohol was extracted at 0.1 per 100 parts of the coating film.
The extraction of polyvinyl alcohol was confirmed. Comparative Production Example 1 200 parts of the aqueous resin dispersion (1) obtained in Production Example 1
After adding 6.3 parts of 25% aqueous ammonia, 150 parts of a 10% aqueous solution of Kuraray Poval PVA-117 was mixed to obtain a comparative aqueous resin dispersion (1). This comparative aqueous resin dispersion (1) has a nonvolatile content of 29.0%, a pH of 8.9, and a viscosity of
It showed a special value of 2200 cps (B-type viscometer) and a minimum film formation temperature of 0°C or less. Production Example 1
When polyvinyl alcohol was extracted using the same method as above, it was confirmed that 12.7 parts of polyvinyl alcohol were extracted per 100 parts of the coating film. Comparative Production Example 2 200 parts of the aqueous resin dispersion (2) obtained in Production Example 2
After adding 5.7 parts of 25% aqueous ammonia, 290 parts of a 10% aqueous solution of Kuraray Poval PVA-205 was added and mixed well to obtain a comparative aqueous resin dispersion (2).
This comparative aqueous resin dispersion (2) has a non-volatile content of 24.6%,
PH9.2, viscosity 36cps (B type viscometer), minimum film forming temperature 45
℃ was shown. When polyvinyl alcohol was extracted from the coating film obtained by applying this comparison aqueous resin dispersion (2) on a Teflon plate in the same manner as in Production Example 1, 23.4 parts of polyvinyl alcohol was extracted per 100 parts of the coating film. Extraction of polyvinyl alcohol was confirmed. Comparative Production Example 3 Kuraray Poval PVA-117 was placed in a separable flask equipped with a stirrer, reflux condenser, and thermometer.
After charging 600 parts of a 10% aqueous solution, the temperature was raised to 70° C. with stirring while blowing nitrogen gas. Thereafter, 8 parts of a 1% aqueous solution of ammonium persulfate was added, and heat treatment was performed at 70°C for 60 minutes. 152 parts of the obtained heat-treated PVA-117 aqueous solution was added to Production Example 1.
After adding to 200 parts of the aqueous resin dispersion (1) obtained in
After thorough mixing, 6.3 parts of 25% aqueous ammonia was added to obtain a comparative aqueous resin dispersion (3). This comparative aqueous resin dispersion (3) has a non-volatile content of 28.9%, a pH of 8.8,
The viscosity was 2080 cps (B-type viscometer), and the minimum film forming temperature was 0°C or less. This comparative aqueous resin dispersion
When polyvinyl alcohol was extracted from the coating film obtained by applying (3) on a Teflon plate in the same manner as in Production Example 1, it was confirmed that 10.9 parts of polyvinyl alcohol were extracted per 100 parts of the coating film. Production Example 1 Aqueous resin dispersions (1) to (3) obtained in Production Examples 1 to 3
Using the comparative aqueous resin dispersions (1) to (3) obtained in Comparative Production Examples 1 to 3, the aqueous resin dispersions (1), (3) and the comparative aqueous resin dispersions (1) to ( 3) as is, and the aqueous resin dispersion (2) as CS- for 100 parts of the dispersion (2).
12 (film-forming aid manufactured by Chitsuso Co., Ltd.) was added to create sealers for inorganic porous substrates (1) to (3) and comparative sealers for inorganic porous substrates (1) to (3), respectively. ), these were coated at 20 g/m 2 on the inorganic porous substrate shown in Table 1, and after drying in a hot air dryer at 120°C for 10 minutes,
The adhesion of the coating film to the substrate, hot water resistance, and frost damage resistance were examined. The results were as shown in Table 1.
【表】【table】
【表】【table】
Claims (1)
以上のポリビニルアルコールおよび重合開始剤か
らなる混合物を、40℃以上の温度で加熱処理して
得られる水性樹脂分散体を含有することを特徴と
する無機多孔質基材用シーラー。 2 ポリビニルアルコールを、アクリル系水性樹
脂分散物100重量部に対し固形分比で1〜30重量
部配合したものである特許請求の範囲第1項に記
載の無機多孔質基材用シーラー。 3 ポリビニルアルコールの重合度が200〜2600
である特許請求の範囲第1または2項に記載の無
機多孔質基材用シーラー。[Claims] 1. Acrylic aqueous resin dispersion, degree of saponification 80 mol%
A sealer for an inorganic porous substrate, characterized in that it contains an aqueous resin dispersion obtained by heat-treating a mixture consisting of the above polyvinyl alcohol and a polymerization initiator at a temperature of 40° C. or higher. 2. The sealer for inorganic porous substrates according to claim 1, which contains polyvinyl alcohol in a solid content ratio of 1 to 30 parts by weight based on 100 parts by weight of an acrylic aqueous resin dispersion. 3 The degree of polymerization of polyvinyl alcohol is 200 to 2600
The sealer for inorganic porous substrates according to claim 1 or 2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62275850A JPS6445472A (en) | 1987-04-24 | 1987-11-02 | Aqueous resin dispersion and sealer containing same for inorganic porous substrate |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9964987 | 1987-04-24 | ||
| JP62275850A JPS6445472A (en) | 1987-04-24 | 1987-11-02 | Aqueous resin dispersion and sealer containing same for inorganic porous substrate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6445472A JPS6445472A (en) | 1989-02-17 |
| JPH0573137B2 true JPH0573137B2 (en) | 1993-10-13 |
Family
ID=14252902
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62275850A Granted JPS6445472A (en) | 1987-04-24 | 1987-11-02 | Aqueous resin dispersion and sealer containing same for inorganic porous substrate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6445472A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5530021B2 (en) * | 1973-03-20 | 1980-08-07 |
-
1987
- 1987-11-02 JP JP62275850A patent/JPS6445472A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6445472A (en) | 1989-02-17 |
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