JPH0237207B2 - - Google Patents
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- JPH0237207B2 JPH0237207B2 JP56073888A JP7388881A JPH0237207B2 JP H0237207 B2 JPH0237207 B2 JP H0237207B2 JP 56073888 A JP56073888 A JP 56073888A JP 7388881 A JP7388881 A JP 7388881A JP H0237207 B2 JPH0237207 B2 JP H0237207B2
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Description
本発明は疎水性基と親水性基とを有する特定の
変性ポリビニルアルコール(以下ポリビニルアル
コールを単にPVAと略記する)を乳化分散剤と
して用い、ラジカル重合性を有しない親油性非水
溶性物質を乳化分散する方法に関する。
化粧品、農薬、合成樹脂接着剤、各種バインダ
ー切削用油剤などの製造に際しては水性媒体中に
親油性非水溶性物質を乳化分散させる場合が多く
ある。この場合乳化分散剤として一般には低分子
の界面活性剤が多く使用されている。低分子の界
面活性剤を適当に選択すればある程度安定な乳化
物は得られるものの低温においた時の安定性であ
るとか機械的な剪断力がかかつた時の安定性等に
しばしば劣る場合があり、冬期の貯蔵中における
増粘ゲル化、やポンプによる移送あるいはスプレ
ツダーロールによる塗布などの際に粗粒が発生す
るとか、粘度が大きく変動するなど実用上の問題
を生じる場合がある。又、低分子活性剤を多量に
使用すれば以上のごとき安定性の上での問題は解
決する方向にはあるものの得られた皮膜中に多量
の活性剤が含有されることになり接着性能とか皮
膜の耐水性とかが大巾に低下し実用上非常に大き
な問題となる。さらに低分子活性剤を使用した時
は低粘度の乳化物しか得られない等の種々の問題
があり、高分子界面活性剤を用いた乳化方法の開
発が待たれているところである。PVAは水溶性
の高分子物質であり、かつ強靭な皮膜を形成する
などの面から種々の工業的利用が行なわれてい
る。しかしながら主鎖の炭素骨格に水酸基及び酢
酸基の単純な置換基をのみ有するものである為
か、充分な界面活性能を有したものではなく、そ
れを乳化分散剤とした乳化分散方法には多くの困
難がともなうものである。
この様な実状にかんがみ、本発明者等は先に(A)
炭素数が6以上の脂肪酸ビニルエステル、炭素数
が6以上のアルキルビニルエーテル及び炭素数が
6以上のα−オレフインよりなる群より選ばれる
単量体の少くとも一種と、(B)エチレン性不飽和カ
ルボン酸もしくはその低級アルキルエステル又は
酸無水物の少くとも一種及び(C)酢酸ビニルエステ
ルの三成分を必須成分とする共重合体をアルコー
ル溶液中で鹸化して得られるポリビニルアルコー
ル系共重合体をエチレン性不飽和単量体の重合過
程で保護コロイドとして用いることにより、高粘
度かつ低構造粘性であり、かつ放置安定性、凍結
融解安定性、高温安定性、添加物に対する安定性
等いずれの性質においてもすぐれた樹脂エマルジ
ヨンが得られるという事実を見出し特願昭53−
44419(特開昭54−135882号)として特許出願を行
なつている。一般に乳化重合とは水溶性ラジカル
開始剤と乳化剤を用いて重合性単量体を重合する
ものである。乳化重合における乳化剤とか保護コ
ロイドの作用機構は必ずしも明確ではないが乳化
重合における乳化剤の役目はまず第一には重合の
場の提供ということにある。乳化重合においては
この乳化剤の可溶化作用によつて重合性単量体が
可溶化される。可溶化された単量体に水溶性ラジ
カル開始剤が攻撃することによつて重合が開始さ
れる。この可溶化作用がない場合は水溶性ラジカ
ルが単量体を攻撃し得ないので円滑な重合は進行
しない。さらに酢酸ビニルエステルのごとき単量
体にあつてはPVA系重合体を乳化剤、保護コロ
イドとして重合する場合酢酸ビニルエステルと
PVA系重合体との間にグラフト重合体を生成し
それが樹脂エマルジヨンの安定性とか実用物性に
大きな影響をおよぼすものである。一方本願発明
のごとき乳化分散方法はいわゆる後乳化とよばれ
ているものであり、水性媒体中に親油性非水溶性
物質を機械的な力などで分散せしめるものであり
乳化剤の作用はもつぱら分散相と水相との界面エ
ネルギーを低下させることにより安定化するもの
である。そこでは親油性非水溶性物質の「ぬれ」
に注目し乳化剤のいわゆるHLBが考慮されるも
のである。
界面活性剤は湿潤作用、洗浄作用、乳化分散作
用、可溶化作用、消泡・起泡作用、触媒作用、帯
電防止作用等多くの作用があり必ずしもその理論
的根拠は明確ではないが、可溶化作用にあつては
同族列にあつては親油性基の大きいものすなわち
炭素数の大きいアルキル基を有するものの方が可
溶化能が大きいものであり又、HLBはいわば疎
水性基の大きさと親水性基の大きさのバランスと
でもいうべきものである。さらに乳化重合におい
ては前述のごときグラフト重合の影響があるなど
乳化重合といわゆる後乳化とは技術的には全く別
の分野をなすものでありまた産業界にあつては乳
化重合工業と後乳化工業とは、前者が接着剤や塗
料などの産業分野、後者が化粧品、農薬、潤かつ
油などの産業分野においてそれぞれ主としてその
技術が生かされている実情に鑑みれば後乳化技術
としての確立は乳化重合技術におけるそれとは異
なつた工業的意義を有するものである。
しかるに本発明者等は先に開発した乳化重合法
において保護コロイドとして用いたのと同種の変
性ポリビニルアルコールを他の技術分野に応用す
るべく種々研究を重ねた結果、以下に述べるよう
な特定の要件を満たす変性PVAを用いればラジ
カル重合性を有しない親油性非水溶性物質を水性
媒体中に乳化分散せしめることができ、得られた
乳化分散物は安定性に富み、貯蔵性、機械的特性
等にすぐれておりかつ接着性能等の実用物性にも
すぐれたものであることを見出し、本発明に到つ
たものである。即ち本発明は
(A) 炭素数が5以上の脂肪酸のビニルエステル、
炭素数が4以上のアルキル基のビニルエーテル
および炭素数が6以上のα−オレフインよりな
る群から選ばれた単量体の少なくとも一種、
(B) エチレン性不飽和カルボン酸もしくはその低
級アルキルエステル又は酸無水物の少なくとも
1種及び
(C) 酢酸ビニルエステル
の三成分を必須共重合成分として含む共重合体の
ケン化物であつてかつ下記()式を満足する変
性ポリビニルアルコールを乳化分散剤として水性
媒体中にラジカル重合性を有しない親油性非水溶
性物質を乳化分散することからなる乳化分散方法
である。
0.1D50 ()
D=nA+(1−Δ)C/27.5/lB
但し、Aは(A)成分の共重合割合(モル基準)で
あり0.05モル%以上、Bは(B)成分の共重合割合
(モル基準)であり0.1モル%以上、4.2モル%以
下、Cは(C)成分の共重合割合(モル基準)であり
50モル%以上、nは4以上の整数であるが(A)成分
が脂肪酸のビニルエステルの時n=脂肪酸の炭素
数−1、(A)成分がアルキルビニルエーテルの時n
=アルキル基の数、(A)成分がα−オレフインの時
n=α−オレフインの炭素数−2、lは(B)成分中
のカルボキシル基の数、△は(C)成分のケン化割合
(モル基準)であり△=ケン化された(C)成分/(C)成分
をそ
れぞれ示す。
本発明において(A)成分として用いる炭素数が5
以上の脂肪酸のビニルエステルとしては例えばバ
レリン酸ビニルエステル カプリル酸ビニルエス
テル ミリスチン酸ビニルエステル ステアリン
酸ビニルエステルなどがあげられ、なかんずくビ
バリン酸ビニルエステル1,1,3,3テトラメ
チル酪酸ビニルエステルあるいは平均炭素数が10
の飽和分岐状脂肪酸ビニルエステルなどの分岐状
アルキル基を有す脂肪酸ビニルエステルが好適で
ある。炭素数が4以下では安定性の良好な乳化物
は得られ難い。また炭素数が4以上のアルキルの
ビニルエーテルとしてはブチルビニルエーテル、
オクチルビニルエーテル、ラウリルビニルエーテ
ル等がある。なかでもイソアミルビニルエーテル
のごとき分岐状アルキル基を有すビニルエーテル
が好適である。炭素数が3以下では安定性の良好
な乳化物は得られ難い。また炭素数が6以上のα
−オレフインとしてはヘプテン−1、オクテン−
1、ドデセン−1などが好適である。炭素数5以
下では乳化物の安定性が悪く適用できない。前述
した炭素数4以上のアルキル基としては分岐状ア
ルキル基であることが、安定性に富む乳化物が得
られるのでより好適に用いられる。この理由は明
確ではないがアルキル基中のメチル基、メチレン
基、メチン基の比が分岐状アルキル基と直鎖状ア
ルキル基とでは異なることや結晶性、配向性、会
合性などの差に起因するのではないかと考えられ
る。
さらに(B)成分として用いるエチレン性不飽和カ
ルボン酸もしくはその低級アルキルエステル又は
酸無水物としては、アクリル酸、メタクリル酸、
クロトン酸、マレイン酸、イタコン酸、アクリル
酸エチルエステル、メタクリル酸メチルエステ
ル、クロトン酸メチルエステル、シトラコン酸、
シトラコン酸ジエチルエステル、マレイン酸、マ
レイン酸モノメチルエステル、マレイン酸ジエチ
ルエステル、イタコン酸ジメチルエステル、無水
マレイン酸、アコニツト酸などが使用されるが、
シトラコン酸、マレイン酸、イタコン酸、マレイ
ン酸モノメチルエステル、無水マレイン酸が好適
に使用さるが、マレイン酸、無水マレイン酸、マ
レイン酸モノメチルエステル、イタコン酸を用い
た方が乳化物の安定性が大きく、さらに好適であ
る。この理由は明確ではないが、(C)及び(A)成分と
の重合性とか導入されたカルボキシル基の相互の
位置関係などが変性PVAの性能に影響している
のではないかと考えられる。
本発明において使用される変性PVAは前述し
た(A)、(B)および(C)の三成分を必須成分として共重
合により得られる共重合体に含まれる(A)(B)(C)の三
成分の共重合割合及び(C)成分のアセチル基のケン
化の割合は対象とする前述の親油性非水溶性物質
によつても異なるが下記の()式の範囲内から
選択される。
0.1D50 ………()
D=nA+(1−△)C/27.5/lB
但し
A;(A)成分の共重合割合(モル基準)であり0.05
モル%以上
B;(B)成分の共重合割合(モル基準)であり0.1
モル%以上、4.2モル%以下
C;(C)成分の共重合割合(モル基準)50モル%以
上
n;4以上の数であり
(A)成分が脂肪酸のビニルエステルの時
n=脂肪酸の炭素数−1
(A)成分がアルキビニルエーテルの時
n=アルキル基の数
(A)成分がα−オレフインの時
n=α−オレフインの炭素数−2
l;(B)成分中のカルボキシル基の数
△;(C)成分のケン化割合(モル基準)であり
△=ケン化された(C)成分/(C)成分
上記()式の範囲を越えた変性PVAを使用
した場合、親油性非水溶性物質の乳化分散が、充
分におこなわれないかあるいはたとえ何とか乳化
分散しえたとしても得られた乳化分散物の安定性
が悪く本発明の目的を満足しないものである。そ
の理由は変性PVAにあつて主として(A)成分と未
ケン化の(C)成分にもとづく疎水性と主として(B)成
分に基づく親水性とのバランスがくずれもはや乳
化分散安定性を保ち得ない為であると考えられ
る。
さらに本発明は前述した()式を満足する変
性PVAを使用することによつてのみ効果的に乳
化分散を行なうことができるものであり、モル基
準で変性PVA全体を100とした時、(A)成分にあつ
ては0.05モル%、(B)成分にあつては0.1モル%未
満、または4.2モル%より大でであるともはや安
定な乳化物を得ることは出来ない。また(C)成分が
50モル%以下である場合には変性PVAはもはや
PVAが本来有している強い造膜性を失なつてし
まい、そのためか得られた乳化物は接着性能など
の実用物性の低下をきたすこととなる。本発明に
おいて使用される変性PVAは前述した(A)、(B)、
(C)の三成分を必須成分とする共重合体のケン化物
であるが本発明の目的をそこなわない範囲で他の
共重合成分、例えばメタクリルアミド、N−置換
メタクリルアミドアクリルアミド、N−置換アク
リルアミド、N−ビニルピロリドン、炭素数が3
以下のアルキル基のビニルエーテル、炭素数が5
以下のオレフインなどをも共重合成分として前記
(A)、(B)、(C)の三成分に加えて共重合せしめた共重
合体のケン化物を使用することは何等差しつかえ
ない。
本発明に用いる変性PVAの製造には、とくに
困難な点はなく、従来公知の重合方法およびケン
化方法を適用することが出来る。すなわち、重合
方法としては、(A)、(B)および(C)成分をそれぞれの
共重合反応性比に応じて一括もしくは分割的ある
いは連続的に、重合系に投入し、無溶剤下もしく
は水性媒体中あるいはメチルアルコール、エチル
アルコール等の低級アルコールの共存下で、2,
2′−アゾビスイソブチロニトリル、過酸化ベンゾ
イル等のラジカル重合触媒によつて重合する方法
が適用できる。このようにして得られる(A)、(B)お
よび(C)成分を含む共重合体をケン化する方法とし
ては、ポリ酢酸ビニル共重合体のケン化に用いら
れる多くの公知方法が適用できるが、通常は、ア
ルコール溶剤あるいは含水アルコール溶剤中で、
ナトリウムアルコラート、苛性ソーダ、苛性カリ
等のアルカリを作用させてケン化する方法が適当
である。アルコールとしては、メチルアルコー
ル、エチルアルコール等の低級アルコールが特に
好適である。また、これらのアルコール溶剤は、
40重量%以下のアセトン、酢酸メチルエステル、
酢酸エチルエステル、ベンゼン等の低誘電率の溶
剤を含んでいてもよい。
本発明において使用される変性PVAの重合度
はその使用目的によつて適宜選択すべきである
が、通常100〜3000の範囲内が適当である。
本発明の乳化分散方法においてその乳化の対象
となるラジカル重合性を有しない親油性非水溶性
物質は例えばスピンドル油、マシン油、ギヤ油な
どの潤滑油類、パラフインワツクス、流動パラフ
イン、アスフアルトなどの石油製品類、ジオクチ
ルセバケート、ジブチルフタレートなどの可塑剤
類、クレオソート油、コールタールなどのタール
製品類、テレピン油、トール油、ロジンなどの天
然薬品類、大豆油、ヒマシ油などの油脂類、ベン
ゼン、トルエン、キシレンなどの芳香族炭化水素
類、パラフイン類、ハロゲン化炭化水素類、メチ
ルn−アミルケトン、ジ−n−プロピルケトンな
どのケトン類、エーテル類、キシレンジイソシア
ネート、トリメチロールプロパン−トリレンジイ
ソシアネートアダクトなどのイソシアネート類、
カプロン酸、リノレイン酸などの高級脂肪酸類、
オレイルアルコール、セチルアルコールなどの高
級アルコール、ポリエチレン、ポリプロピレン、
ポリ塩化ビニル、ポリエステル、エチレン−酢酸
ビニル共重合体及びそのケン化物、ポリ酢酸ビニ
ルエステル、各種合成ゴムなどの合成樹脂類など
があげられるがこれらに限定されるものではなく
ラジカル重合性を有しない親油性非水溶性物質の
乳化分散に対して広く使用することができる。
乳化分散にあたつては従来公知の手法が採用さ
れる。例えば一般流体撹拌機、高速回転強せん断
型撹拌分散機、コロイドミル、加圧ノズル式乳化
機、スクリユー押出機、超音波式乳化機、機械的
振動撹拌機、静電場を利用した撹拌機等を使用す
る手法で行うことができる。
又、乳化分散剤の添加にあたつては、その方法
に特に制限はなく、乳化分散剤を水に配合し、一
括又は逐次、さらには連続的に親油性非水溶性物
質に添加混合していく手法、親油性非水溶性物質
に乳化分散剤を配合せしめてから水と混合する手
法さらには三者を同時に添加する手法等がある。
乳化分散剤としての変性PVAの配合割合は特
に制限はないが、前述した親油性非水溶性物質に
対して1から30重量%の範囲で配合した場合がこ
のましいがこれに勿論限定するものではない。
本発明の方法を実施するにあたり他種の添加物
例えば脂肪酸ソーダ石ケン、アルキルエーテルサ
ルフエート、ベンジルトリメチルアンモニウムク
ロライド、ジオクチルスルホコハク酸ソーダなど
のイオン性界面活性剤、ポリオキシエチレンオレ
イルエーテル、ソルビタンモノステアレートオキ
シエチレンオキシプロピレンブロツクポリマー、
グリセロールモノステアレートなどの非イオン性
界面活性剤、さらにはポリアクリル酸ソーダ、ポ
リアクリルアミド、未変性又は変性PVA、セル
ロース誘導体などの水溶性高分子類、とか、その
他消泡剤、防カビ剤、防錆剤等の公知の添加剤な
どを本発明の目的をそこなわない範囲で添加使用
することは何らさしつかえない。
この様にして得られたラジカル重合性を有しな
い親油性非水溶性物質の乳化分散物は安定性に富
み又合成樹脂などの乳化物にあつてはすぐれた皮
膜を得ることができるなど、大きな工業的意味を
有し、産業の発展に寄与する所が甚大である。
以下に本発明を実施例によりさらに詳しく説明
するがこれに限定されるものではない。尚実施例
中の部は特にことわらない限り重量基準である。
実施例1〜3、比較例1〜3
表−1に記載された各種の共重合成分を含む変
性PVAを用いて次のごとくその乳化性能を調べ
た。即ち変性PVA20部を水500部に溶解せしめた
後25℃においてホモミキサーで撹拌しながらヒマ
シ油400部を徐々に加え乳化物を得た。ただちに
半径3cm、高さ50cmのフタ付容器に乳化物を入れ
25℃で放置し結果を乳化層の全高に対する100分
率で示した。結果は表−1に記す。実施例1、
2、3ともに安定な乳化物であり、いずれも20日
間経過後もまつたく乳化層の分離がなかつた。(B)
成分に無水マレイン酸を用いた実施例2では30日
経過後も乳化状態をたもつていた。(A)成分が0.05
モル%より少いか(B)成分が0.1モル%より少いか
又は両者を使用しない比較例1、2、3では一旦
乳化状になるが1〜3日で乳化が崩壊されまつた
く安定性が悪かつた。
The present invention uses specific modified polyvinyl alcohol (hereinafter referred to simply as PVA) having a hydrophobic group and a hydrophilic group as an emulsifying and dispersing agent to emulsify a lipophilic water-insoluble substance that does not have radical polymerizability. Concerning how to disperse. In the production of cosmetics, agricultural chemicals, synthetic resin adhesives, various binder cutting oils, etc., lipophilic water-insoluble substances are often emulsified and dispersed in an aqueous medium. In this case, low-molecular surfactants are generally used as emulsifying and dispersing agents. Although it is possible to obtain a somewhat stable emulsion by appropriately selecting a low-molecular surfactant, the stability at low temperatures or when subjected to mechanical shearing force is often inferior. However, practical problems may occur, such as thickening and gelation during winter storage, generation of coarse particles during transfer using a pump, or application using a spreader roll, and large fluctuations in viscosity. Furthermore, although using a large amount of a low-molecular-weight activator may solve the above stability problems, a large amount of the activator will be contained in the resulting film, resulting in poor adhesion performance. The water resistance of the film is greatly reduced, which is a very serious problem in practice. Furthermore, there are various problems such as the fact that only low-viscosity emulsions can be obtained when low-molecular surfactants are used, and the development of an emulsification method using high-molecular surfactants is awaited. PVA is a water-soluble polymeric substance, and is used in various industrial applications because of its ability to form tough films. However, perhaps because it has only simple substituents of hydroxyl and acetate groups on the carbon skeleton of its main chain, it does not have sufficient surface-active ability, and is not used in many emulsifying and dispersing methods using it as an emulsifying dispersant. This is accompanied by many difficulties. In view of these actual circumstances, the inventors first proposed (A)
At least one monomer selected from the group consisting of fatty acid vinyl esters having 6 or more carbon atoms, alkyl vinyl ethers having 6 or more carbon atoms, and α-olefins having 6 or more carbon atoms, and (B) ethylenically unsaturated. A polyvinyl alcohol copolymer obtained by saponifying a copolymer containing at least one of carboxylic acid or its lower alkyl ester or acid anhydride and (C) vinyl acetate as essential components in an alcohol solution. By using it as a protective colloid in the polymerization process of ethylenically unsaturated monomers, it has high viscosity and low structural viscosity, as well as properties such as storage stability, freeze-thaw stability, high temperature stability, and stability against additives. He discovered the fact that excellent resin emulsions could be obtained even in
A patent application has been filed as 44419 (Japanese Unexamined Patent Publication No. 135882/1982). Generally, emulsion polymerization involves polymerizing polymerizable monomers using a water-soluble radical initiator and an emulsifier. Although the mechanism of action of emulsifiers and protective colloids in emulsion polymerization is not necessarily clear, the role of emulsifiers in emulsion polymerization is first of all to provide a site for polymerization. In emulsion polymerization, the polymerizable monomer is solubilized by the solubilizing action of the emulsifier. Polymerization is initiated by the attack of the water-soluble radical initiator on the solubilized monomer. Without this solubilizing effect, water-soluble radicals would not be able to attack the monomers and smooth polymerization would not proceed. Furthermore, in the case of monomers such as vinyl acetate, when PVA-based polymers are used as emulsifiers and protective colloids, vinyl acetate and
A graft polymer is formed between the resin and the PVA polymer, which has a large effect on the stability and practical properties of the resin emulsion. On the other hand, the emulsification and dispersion method of the present invention is so-called post-emulsification, in which a lipophilic water-insoluble substance is dispersed in an aqueous medium by mechanical force, and the effect of the emulsifier is mainly to disperse it. Stabilization is achieved by lowering the interfacial energy between the phase and the aqueous phase. There, "wetting" of lipophilic water-insoluble substances
Focusing on this, the so-called HLB emulsifier is considered. Surfactants have many functions such as wetting, cleaning, emulsifying and dispersing, solubilizing, antifoaming/foaming, catalytic, and antistatic functions, and although the theoretical basis for these functions is not necessarily clear, they are effective in solubilizing. In terms of action, in the homologous series, those with larger lipophilic groups, that is, those with alkyl groups with a larger number of carbon atoms, have greater solubilizing ability, and HLB depends on the size of the hydrophobic group and the hydrophilicity. It can be said to be a balance of basic sizes. Furthermore, in emulsion polymerization, there is the influence of graft polymerization as mentioned above, and emulsion polymerization and so-called post-emulsification are technically completely different fields, and in industry, emulsion polymerization industry and post-emulsification industry are In view of the fact that the former is mainly used in industrial fields such as adhesives and paints, and the latter is mainly used in industrial fields such as cosmetics, agricultural chemicals, and oils, emulsion polymerization is the most established post-emulsification technology. It has an industrial significance different from that in technology. However, as a result of repeated research in order to apply the same type of modified polyvinyl alcohol used as a protective colloid in the emulsion polymerization method developed earlier, the present inventors have found that the following specific requirements have been met. If modified PVA that satisfies the above criteria is used, it is possible to emulsify and disperse lipophilic water-insoluble substances that do not have radical polymerizability in an aqueous medium, and the resulting emulsified dispersion has excellent stability, storage stability, mechanical properties, etc. The present inventors have discovered that it has excellent practical properties such as adhesion performance, and has developed the present invention. That is, the present invention provides (A) a vinyl ester of a fatty acid having 5 or more carbon atoms;
At least one monomer selected from the group consisting of vinyl ethers of alkyl groups having 4 or more carbon atoms and α-olefins having 6 or more carbon atoms; (B) ethylenically unsaturated carboxylic acid or its lower alkyl ester or acid; An aqueous medium using a modified polyvinyl alcohol as an emulsifying dispersant, which is a saponified product of a copolymer containing as essential copolymerization components at least one kind of anhydride and (C) vinyl acetate ester, and which satisfies the following formula (). This is an emulsification and dispersion method consisting of emulsification and dispersion of a lipophilic water-insoluble substance that does not have radical polymerizability. 0.1D50 () D=nA+(1-Δ)C/27.5/lB However, A is the copolymerization ratio of component (A) (on a molar basis), which is 0.05 mol% or more, and B is the copolymerization ratio of component (B). (on a molar basis) is 0.1 mol% or more and 4.2 mol% or less, C is the copolymerization ratio of component (C) (on a molar basis)
50 mol% or more, n is an integer of 4 or more, but when component (A) is a vinyl ester of a fatty acid, n = number of carbon atoms in the fatty acid - 1, and when component (A) is an alkyl vinyl ether, n
= number of alkyl groups, when component (A) is α-olefin, n = number of carbon atoms in α-olefin −2, l is the number of carboxyl groups in component (B), △ is the saponification ratio of component (C) (on a molar basis) and △ = saponified component (C)/component (C), respectively. In the present invention, the number of carbon atoms used as component (A) is 5.
Vinyl esters of the above fatty acids include, for example, vinyl valerate, vinyl caprylate, vinyl myristate, vinyl stearate, among others, vinyl bivalate 1,1,3,3-tetramethylbutyric acid vinyl ester, and average carbon number is 10
Fatty acid vinyl esters having a branched alkyl group, such as saturated branched fatty acid vinyl esters, are preferred. If the number of carbon atoms is 4 or less, it is difficult to obtain an emulsion with good stability. In addition, as vinyl ether of alkyl having 4 or more carbon atoms, butyl vinyl ether,
Examples include octyl vinyl ether and lauryl vinyl ether. Among them, vinyl ethers having a branched alkyl group such as isoamyl vinyl ether are preferred. If the number of carbon atoms is 3 or less, it is difficult to obtain an emulsion with good stability. Also, α with carbon number of 6 or more
-Olefins include heptene-1 and octene-
1, dodecene-1, and the like are preferred. If the number of carbon atoms is 5 or less, the stability of the emulsion is poor and it cannot be applied. As the alkyl group having 4 or more carbon atoms, a branched alkyl group is more preferably used because an emulsion with high stability can be obtained. The reason for this is not clear, but it is due to the fact that the ratio of methyl, methylene, and methine groups in the alkyl group is different between branched and straight-chain alkyl groups, and differences in crystallinity, orientation, association, etc. It is thought that they may do so. Further, as the ethylenically unsaturated carboxylic acid or its lower alkyl ester or acid anhydride used as component (B), acrylic acid, methacrylic acid,
Crotonic acid, maleic acid, itaconic acid, ethyl acrylate, methyl methacrylate, methyl crotonic acid, citraconic acid,
Citraconic acid diethyl ester, maleic acid, maleic acid monomethyl ester, maleic acid diethyl ester, itaconic acid dimethyl ester, maleic anhydride, aconitic acid, etc. are used.
Citraconic acid, maleic acid, itaconic acid, maleic acid monomethyl ester, and maleic anhydride are preferably used, but the stability of the emulsion is greater when maleic acid, maleic anhydride, maleic acid monomethyl ester, and itaconic acid are used. , is even more suitable. The reason for this is not clear, but it is thought that the polymerizability with components (C) and (A), the mutual positional relationship of the introduced carboxyl groups, etc. influence the performance of modified PVA. The modified PVA used in the present invention contains (A), (B), and (C) contained in the copolymer obtained by copolymerization with the above-mentioned three components (A), (B), and (C) as essential components. The copolymerization ratio of the three components and the saponification ratio of the acetyl group of component (C) vary depending on the target lipophilic water-insoluble substance, but are selected from within the range of formula () below. 0.1D50 ......() D=nA+(1-△)C/27.5/lB However, A: Copolymerization ratio of component (A) (molar basis), which is 0.05
Mole% or more B: Copolymerization ratio of component (B) (molar basis), which is 0.1
mol% or more, 4.2 mol% or less Number-1 (A) When component is an alkyl ether, n = number of alkyl groups (A) When component is α-olefin, n = number of carbon atoms in α-olefin – 2 l; (B) Number of carboxyl groups in component △: Saponification ratio (mole basis) of component (C) △=Saponified component (C)/component (C) When using modified PVA that exceeds the range of formula () above, lipophilic non-lipophilic The emulsification and dispersion of the water-soluble substance may not be sufficiently carried out, or even if it can be emulsified and dispersed, the stability of the obtained emulsion dispersion is poor and the object of the present invention cannot be achieved. The reason for this is that in modified PVA, the balance between hydrophobicity, which is mainly based on component (A) and unsaponified component (C), and hydrophilicity, which is mainly based on component (B), is lost, and emulsion dispersion stability can no longer be maintained. This is thought to be due to the Furthermore, in the present invention, effective emulsification and dispersion can only be carried out by using modified PVA that satisfies the above-mentioned formula (2), and when the entire modified PVA is taken as 100 on a molar basis, If the amount is less than 0.05 mol% for component () and 0.1 mol% or more than 4.2 mol% for component (B), it is no longer possible to obtain a stable emulsion. Also, component (C)
Modified PVA is no longer present if less than 50 mol%
The strong film-forming properties that PVA originally possesses are lost, and the resulting emulsion suffers from a decline in practical physical properties such as adhesive performance. The modified PVA used in the present invention is as described above (A), (B),
A saponified product of a copolymer having the three components (C) as essential components, but other copolymer components such as methacrylamide, N-substituted methacrylamide, acrylamide, N-substituted Acrylamide, N-vinylpyrrolidone, 3 carbons
Vinyl ether of the following alkyl group, carbon number is 5
The following olefins are also used as copolymerization components.
In addition to the three components (A), (B), and (C), there is no problem in using a saponified copolymer obtained by copolymerization. There are no particular difficulties in producing the modified PVA used in the present invention, and conventionally known polymerization methods and saponification methods can be applied. In other words, as a polymerization method, components (A), (B), and (C) are added to a polymerization system all at once, in parts, or continuously depending on their respective copolymerization reactivity ratios, and the In a medium or in the presence of lower alcohols such as methyl alcohol and ethyl alcohol, 2.
A method of polymerization using a radical polymerization catalyst such as 2'-azobisisobutyronitrile or benzoyl peroxide can be applied. As a method for saponifying the copolymer containing components (A), (B), and (C) obtained in this way, many known methods used for saponifying polyvinyl acetate copolymers can be applied. However, usually in an alcoholic solvent or a hydroalcoholic solvent,
A suitable method is saponification using an alkali such as sodium alcoholate, caustic soda, or caustic potash. As the alcohol, lower alcohols such as methyl alcohol and ethyl alcohol are particularly suitable. In addition, these alcohol solvents are
Not more than 40% by weight of acetone, acetic acid methyl ester,
It may also contain a low dielectric constant solvent such as ethyl acetate or benzene. The degree of polymerization of the modified PVA used in the present invention should be appropriately selected depending on its intended use, but is usually within the range of 100 to 3,000. In the emulsification and dispersion method of the present invention, lipophilic water-insoluble substances that do not have radical polymerizability and are to be emulsified include, for example, lubricating oils such as spindle oil, machine oil, and gear oil, paraffin wax, liquid paraffin, and asphalt. petroleum products, plasticizers such as dioctyl sebacate and dibutyl phthalate, tar products such as creosote oil and coal tar, natural chemicals such as turpentine oil, tall oil, and rosin, oils and fats such as soybean oil and castor oil. aromatic hydrocarbons such as benzene, toluene, and xylene, paraffins, halogenated hydrocarbons, ketones such as methyl n-amyl ketone and di-n-propyl ketone, ethers, xylene diisocyanate, and trimethylolpropane. Isocyanates such as tolylene diisocyanate adduct,
Higher fatty acids such as caproic acid and linoleic acid,
Higher alcohols such as oleyl alcohol and cetyl alcohol, polyethylene, polypropylene,
Examples include, but are not limited to, synthetic resins such as polyvinyl chloride, polyester, ethylene-vinyl acetate copolymer and saponified products thereof, polyvinyl acetate ester, and various synthetic rubbers, and do not have radical polymerizability. It can be widely used for emulsifying and dispersing lipophilic water-insoluble substances. For emulsification and dispersion, conventionally known methods are employed. For example, general fluid stirrers, high-speed rotation, strong shear type stirring and dispersion machines, colloid mills, pressure nozzle emulsifiers, screw extruders, ultrasonic emulsifiers, mechanical vibration stirrers, stirrers that use electrostatic fields, etc. This can be done using the method you use. In addition, when adding an emulsifying dispersant, there is no particular restriction on the method, and the emulsifying dispersing agent may be blended with water and then added and mixed with the lipophilic water-insoluble substance all at once, sequentially, or even continuously. There are several methods, including a method in which an emulsifying dispersant is blended with a lipophilic water-insoluble substance and then mixed with water, and a method in which all three are added at the same time. There is no particular restriction on the blending ratio of modified PVA as an emulsifying dispersant, but it is preferably blended in a range of 1 to 30% by weight based on the lipophilic water-insoluble substance mentioned above, but it is of course limited to this range. isn't it. Other types of additives may be used in carrying out the process of the invention, such as fatty acid soda soaps, alkyl ether sulfates, benzyltrimethylammonium chloride, ionic surfactants such as dioctyl sodium sulfosuccinate, polyoxyethylene oleyl ether, sorbitan monostearer, etc. rate oxyethylene oxypropylene block polymer,
Nonionic surfactants such as glycerol monostearate, water-soluble polymers such as sodium polyacrylate, polyacrylamide, unmodified or modified PVA, cellulose derivatives, and other antifoaming agents, antifungal agents, There is no problem in adding known additives such as rust preventives to the extent that they do not impair the purpose of the present invention. The emulsified dispersion of a lipophilic water-insoluble substance that does not have radical polymerizability obtained in this way is highly stable, and when used with emulsions of synthetic resins, it is possible to obtain excellent films. It has industrial significance and greatly contributes to the development of industry. EXAMPLES The present invention will be explained in more detail with reference to examples below, but the present invention is not limited thereto. Note that parts in the examples are based on weight unless otherwise specified. Examples 1 to 3, Comparative Examples 1 to 3 Modified PVA containing the various copolymer components listed in Table 1 was used to examine its emulsifying performance as follows. That is, 20 parts of modified PVA was dissolved in 500 parts of water, and then 400 parts of castor oil was gradually added at 25° C. while stirring with a homomixer to obtain an emulsion. Immediately pour the emulsion into a lidded container with a radius of 3 cm and a height of 50 cm.
The results were expressed as a percentage of the total height of the emulsified layer after being left at 25°C. The results are shown in Table-1. Example 1,
Both emulsions No. 2 and No. 3 were stable emulsions, and no separation of the emulsion layer occurred in either case even after 20 days. (B)
In Example 2, in which maleic anhydride was used as a component, the emulsified state remained even after 30 days. (A) component is 0.05
In Comparative Examples 1, 2, and 3 where the amount of component (B) is less than 0.1 mol% or both are not used, the emulsion becomes an emulsion, but the emulsion collapses in 1 to 3 days and the stability is poor. It was.
【表】
実施例4〜5、比較例4〜8
ステアリルアルコール50部、変性PVA10部、
水140部を撹拌機付容器に投入し85℃に加温して
600回転/分の速度で2時間撹拌する。撹拌をつ
づけながら20分間で25℃にまで冷却してから内容
物をとり出した。結果は表−2に記した通りであ
る。
(A)成分としてラウリルビニルエーテル、(B)成分
としてクロトン酸を用いた時のD=14.9、また(A)
成分としてステアリルビニルエーテル、(B)成分と
してクロトン酸を用いた時のD=47.5では良好な
乳化物が得られたが、D=56.2またD=138.3で
は水層が分離しており良好な乳化物は得られなか
つた。又、(A)、(B)のどちらか一方の成分を使用し
ない時は粗大粒子が多く良好な乳化物は得られな
かつた。さらに(A)成分としてアルキル基の炭素数
が2であるエチルビニルエーテルを用い(B)成分に
クロトン酸を用いた時も粗大粒子が多く、良好な
乳化物は得られなかつた。[Table] Examples 4-5, Comparative Examples 4-8 50 parts of stearyl alcohol, 10 parts of modified PVA,
Pour 140 parts of water into a container with a stirrer and heat to 85℃.
Stir for 2 hours at a speed of 600 rpm. While stirring was continued, the contents were cooled to 25° C. over 20 minutes and then taken out. The results are shown in Table-2. When using lauryl vinyl ether as component (A) and crotonic acid as component (B), D = 14.9, and (A)
When stearyl vinyl ether was used as a component and crotonic acid was used as component (B), a good emulsion was obtained at D=47.5, but when D=56.2 and D=138.3, the aqueous layer was separated and a good emulsion was obtained. I couldn't get it. Furthermore, when either component (A) or (B) was not used, a good emulsion was not obtained due to the presence of many coarse particles. Further, when ethyl vinyl ether having an alkyl group having 2 carbon atoms was used as component (A) and crotonic acid was used as component (B), there were many coarse particles and a good emulsion could not be obtained.
【表】
実施例6〜9、比較例9〜13
容量60c.c.の開放型混練機を用いて老化防止剤と
して少量の3,5−ジ−t−ブチル−4−ヒドロ
キシトルエンを含有するポリイソプレンゴム(シ
ス1,4−含有98%、トルエン中30℃での極限粘
度3.4dl/g)40gを90℃で15分間混練した後に
各種変性PVA5g及び水5gの混合物を少量づつ
添加しつつ混練した所白色の混練物が得られた。
さらに混練をつづけ5gの水を添加した時点でこ
れを混練機より取り出し50gの水に投入撹拌し、
後の試験に供した。
外観;試料を清浄なガラス板上にガラス棒で
均一に薄く塗布し、ただちに粗粒子および異物
の有無を肉眼で調べた。
低温安定性;試料をポリエチレン製のふた付
容器にとり0℃で16時間保ち、恒温水そう中に
30℃で1時間放置したのちガラス棒でかきまぜ
てそのときの状態を観察。
皮膜性能;厚さ0.5mmになる様あらかじめ秤
取した乳化物を20℃、60%RHの恒温恒湿室中
で水平に保つた板上にて流延作成、上記に得た
皮膜の透明性は肉眼で判定。
実施例6〜9においてずれも粗粒のないきれい
な乳化物が得られ低温安定性も良好であつた。比
較例9ではD=0.07、また比較例10ではD=0.06
でありいずれも本発明の好適な範囲を満足しない
為粗粒の多い乳化状物を得たのみである。
(A)成分として直鎖のアルキ基を有するブチルビ
ニルエーテル、ラウリルビニルエーテルのごとき
単量体を用いた時よりVeoVa−10(シエル化学社
製の平均炭素数10の飽和分岐状脂肪酸のビニルエ
ステル)のごとき分岐状のアルキル基を有する単
量体を使用した時の方が乳化物から得た皮膜の透
明性は良好である。さらに(A)成分(B)成分の両者を
使用しないPVAに加えてポリオキシエチレンノ
ニルフエニルエーテル10部を使用して同様に乳化
操作を行なつたところ、比較例13では良好な乳化
物は一応得られたものの0℃に16時間保つたとこ
ろ全体がゲル化してしまい、まつたく安定性が悪
かつた。さらに得られた皮膜は白濁し、にごりの
大きいものであり、本発明において使用される変
性PVAを使用した時の効果におよぶべくもなか
つた。[Table] Examples 6 to 9, Comparative Examples 9 to 13 Containing a small amount of 3,5-di-t-butyl-4-hydroxytoluene as an antiaging agent using an open kneader with a capacity of 60 c.c. After kneading 40 g of polyisoprene rubber (98% cis-1,4-content, intrinsic viscosity 3.4 dl/g at 30°C in toluene) at 90°C for 15 minutes, a mixture of 5 g of various modified PVA and 5 g of water was added little by little. Upon kneading, a white kneaded product was obtained.
Further kneading was continued and when 5g of water was added, it was taken out from the kneader and poured into 50g of water and stirred.
It was used for later tests. Appearance: The sample was applied thinly and uniformly onto a clean glass plate using a glass rod, and immediately inspected with the naked eye for the presence of coarse particles and foreign matter. Low temperature stability: Place the sample in a polyethylene container with a lid and keep it at 0℃ for 16 hours, then put it in a constant temperature water bath.
After leaving it at 30℃ for 1 hour, stir it with a glass rod and observe the condition at that time. Film performance: Pre-weighed emulsion to a thickness of 0.5 mm was cast on a plate kept horizontally in a constant temperature and humidity room at 20°C and 60% RH.The transparency of the film obtained above was is determined by the naked eye. In Examples 6 to 9, clean emulsions without coarse particles were obtained and the low temperature stability was also good. In Comparative Example 9, D=0.07, and in Comparative Example 10, D=0.06
However, since neither of them satisfied the preferred range of the present invention, only an emulsion containing many coarse particles was obtained. When a monomer such as butyl vinyl ether or lauryl vinyl ether having a linear alkyl group is used as component (A), VeoVa-10 (vinyl ester of saturated branched fatty acid with an average carbon number of 10 manufactured by Ciel Chemical Co., Ltd.) The transparency of the film obtained from the emulsion is better when a monomer having a branched alkyl group is used. Furthermore, when a similar emulsification operation was performed using 10 parts of polyoxyethylene nonyl phenyl ether in addition to PVA that does not use both components (A) and (B), a good emulsion was obtained in Comparative Example 13. Although the obtained product was kept at 0°C for 16 hours, the entire product turned into a gel, and its stability was extremely poor. Furthermore, the film obtained was cloudy and cloudy, and could not achieve the same effect as the modified PVA used in the present invention.
【表】【table】
【表】【table】
Claims (1)
ル、炭素数が4以上のアルキル基のビニルエーテ
ルおよび炭素数が6以上のα−オレフインよりな
る群から選ばれた単量体の少なくとも一種、(B)エ
チレン性不飽和カルボン酸もしくはその低級アル
キルエステル又は酸無水物の少なくとも1種及び
(C)酢酸ビニルエステルの三成分を必須共重合成分
として含む共重合体のケン化物であつてかつ下記
()式を満足する変性ポリビニルアルコールを
乳化分散剤として水性媒体中にラジカル重合性を
有しない親油性非水溶性物質を乳化分散すること
からなる乳化分散方法。 0.1D50 () D=nA+(1−Δ)C/27.5/lB 但し、Aは(A)成分の共重合割合(モル基準)で
あり0.05モル%以上、Bは(B)成分の共重合割合
(モル基準)であり0.1モル%以上、4.2モル%以
下、Cは(C)成分の共重合割合(モル基準)であり
50モル%以上、nは4以上の整数であるが(A)成分
が脂肪酸のビニルエステルの時n=脂肪酸の炭素
数−1、(A)成分がアルキルビニルエーテルの時n
=アルキル基の数、(A)成分がα−オレフインの時
n=α−オレフインの炭素数−2、lは(B)成分中
のカルボキシル基の数、△は変性ポリビニルアル
コール中の(C)成分のケン化割合(モル基準)であ
り、△=ケン化された(C)成分/(C)成分をそれぞれしめ
す。 2 乳化分散剤が(A)成分としてカルボキシル基が
3級もしくは4級の炭素原子に対してα−位に存
在する分岐状脂肪酸ビニルエステル、(B)成分とし
てエチレン性不飽和ジカルボン酸もしくはその低
級アルキルモノエステルないしはジエステル又は
酸無水物を含有している変性ポリビニルアルコー
ルである特許請求の範囲1に記載の乳化分散方
法。 3 B成分がマレイン酸モノメチルエステル又は
無水マレイン酸である特許請求の範囲2に記載の
乳化分散方法。 4 B成分がイタコン酸である特許請求の範囲2
に記載の乳化分散方法。[Scope of Claims] 1 (A) A monomer selected from the group consisting of vinyl esters of fatty acids having 5 or more carbon atoms, vinyl ethers of alkyl groups having 4 or more carbon atoms, and α-olefins having 6 or more carbon atoms. (B) at least one ethylenically unsaturated carboxylic acid or its lower alkyl ester or acid anhydride;
(C) A saponified product of a copolymer containing three components of vinyl acetate as essential copolymerization components, which has radical polymerizability in an aqueous medium using modified polyvinyl alcohol that satisfies the following formula () as an emulsifying dispersant. An emulsification and dispersion method consisting of emulsification and dispersion of lipophilic water-insoluble substances. 0.1D50 () D=nA+(1-Δ)C/27.5/lB However, A is the copolymerization ratio (molar basis) of component (A), which is 0.05 mol% or more, and B is the copolymerization ratio of component (B). (on a molar basis) is 0.1 mol% or more and 4.2 mol% or less, C is the copolymerization ratio of component (C) (on a molar basis)
50 mol% or more, n is an integer of 4 or more, but when component (A) is a vinyl ester of a fatty acid, n = number of carbon atoms in the fatty acid - 1, and when component (A) is an alkyl vinyl ether, n
= number of alkyl groups, when component (A) is α-olefin, n = number of carbon atoms in α-olefin −2, l is the number of carboxyl groups in component (B), △ is (C) in modified polyvinyl alcohol It is the saponification ratio of the components (on a molar basis), and △ = saponified component (C)/component (C), respectively. 2 The emulsifying dispersant contains a branched fatty acid vinyl ester in which the carboxyl group is present at the α-position relative to a tertiary or quaternary carbon atom as the component (A), and an ethylenically unsaturated dicarboxylic acid or its lower class as the component (B). The emulsifying and dispersing method according to claim 1, which is a modified polyvinyl alcohol containing an alkyl monoester or diester or an acid anhydride. 3. The emulsifying and dispersing method according to claim 2, wherein component B is maleic acid monomethyl ester or maleic anhydride. 4 Claim 2 in which component B is itaconic acid
The emulsification dispersion method described in .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56073888A JPS57190642A (en) | 1981-05-15 | 1981-05-15 | Dispersion by emulsification |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56073888A JPS57190642A (en) | 1981-05-15 | 1981-05-15 | Dispersion by emulsification |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57190642A JPS57190642A (en) | 1982-11-24 |
| JPH0237207B2 true JPH0237207B2 (en) | 1990-08-23 |
Family
ID=13531192
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56073888A Granted JPS57190642A (en) | 1981-05-15 | 1981-05-15 | Dispersion by emulsification |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57190642A (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5445687A (en) * | 1977-08-19 | 1979-04-11 | Nippon Synthetic Chem Ind Co Ltd:The | Dispersion stabilizer for suspension polymerization of vinyl compound |
| JPS5445688A (en) * | 1977-08-30 | 1979-04-11 | Nippon Synthetic Chem Ind Co Ltd:The | Dispersion stabilizer for suspension polymerization of binyl compound |
-
1981
- 1981-05-15 JP JP56073888A patent/JPS57190642A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57190642A (en) | 1982-11-24 |
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