JPS647634B2 - - Google Patents

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Publication number
JPS647634B2
JPS647634B2 JP9378483A JP9378483A JPS647634B2 JP S647634 B2 JPS647634 B2 JP S647634B2 JP 9378483 A JP9378483 A JP 9378483A JP 9378483 A JP9378483 A JP 9378483A JP S647634 B2 JPS647634 B2 JP S647634B2
Authority
JP
Japan
Prior art keywords
water
emulsion
weight
cloth
oil
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
Application number
JP9378483A
Other languages
Japanese (ja)
Other versions
JPS59219380A (en
Inventor
Taisuke Matsui
Harumi Tatsu
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.)
Nippon Mektron KK
Original Assignee
Nippon Mektron KK
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 Nippon Mektron KK filed Critical Nippon Mektron KK
Priority to JP9378483A priority Critical patent/JPS59219380A/en
Publication of JPS59219380A publication Critical patent/JPS59219380A/en
Publication of JPS647634B2 publication Critical patent/JPS647634B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、撥水撥油剤エマルジヨンの製造法に
関する。更に詳しくは、乳化剤を含有しない撥水
撥油剤エマルジヨンの製造法に関する。 一般に、撥水撥油剤エマルジヨンは、乳化剤を
用いて製造されている。乳化剤としては、主とし
て次のような理由によつてノニオン系のものが使
用されている。即ち、アニオン系およびカチオン
系の乳化剤は、撥水撥油剤共重合体を構成する共
単量体の種類によつてはラテツクスを不安定化さ
せ易く、特にカチオン系乳化剤の場合、撥水撥油
性能に好結果をもたらすハロゲン化ビニル、ハロ
ゲン化ビニリデンなどを共単量体成分とする共重
合体は、安定性の悪いエマルジヨンしか与えな
い。 また、アニオン系乳化剤の存在は、撥水撥油性
能を著しく損わせる。更に、これらの乳化剤は、
それ自身がイオン性であるため、各種繊維用処理
剤との組成物を自由に調整し得ない。 これに対して、ノニオン系の乳化剤、一般には
分散力にすぐれているためよく用いられているポ
リエチレングリコールアルキルフエノールエーテ
ル、ポリエチレングリコールアルキルエーテル系
などのノニオン系乳化剤は、生分解性に劣り、従
つて廃水処理上の問題を生ずるばかりではなく、
撥水撥油剤共重合体の共単量体としてハロゲン化
ビニル、ハロゲン化ビニリデンなどを選択した場
合には、逆にこの生分解が促進され、これが織物
の変色や着色原因を形成している。 こうした乳化剤の存在による撥水撥油剤エマル
ジヨンの性能低下を避けるために、炭素数8以上
のパーフルオロアルキル基含有重合性化合物およ
びオキシアルキレン単位9以上の親水性基含有重
合性化合物を構成単位として含有する共重合体
を、実質的に乳化剤を使用することなく水性媒体
中に分散せしめた水性分散液が提案され、これは
汚れ脱離性能の改良された撥水撥油剤を与えるこ
とが、特開昭53−134786号公報に記載されてい
る。しかしながら、この撥水撥油剤には、特に撥
水性能の低下がみられ、パーフルオロアルキル基
含有重合性化合物を60重量%含有する共重合体を
用いた場合でも、その撥水性は70、よくても高々
80である。 本発明者らは、乳化剤を含有せず、しかも撥水
撥油性にすぐれた撥水撥油剤エマルジヨンを求め
て種々検討の結果、炭素数3以上のフルオロアル
キル基を含有するビニル単量体を、これと共重合
可能な親水性基を含有しない他のビニル単量体お
よび架橋性単量体を、乳化剤の不存在下に、一価
の低級アルコール、環状エーテルまたは非プロト
ン性極性溶媒である親水性有機溶媒水溶液中でラ
ンダム共重合させることにより、上記課題が解決
された撥水撥油剤エマルジヨンを製造し得ること
を見出した。従つて、本発明は、このようにして
行われる撥水撥油剤の製造法に係るものである。 炭素数3以上のフルオロアルキル基を含有する
ビニル単量体としては、例えば次のような化合物
が挙げられる。ただし、式中Rは2価の有機基で
あり、R′は水素原子またはメチル基であり、
R″は低級アルキル基であり、そしてnは3以上、
一般には3〜20の整数である。 CH2=CR′COORCoF2o+1 CH2=CR′COOCH2CH2C6F13 CH2=CR′COOCH2CH2C8F17 CH2=CR′COOCH2CH2C10F21 CH2=CR′COOCH2CH2C12F25 また、これと共重合可能な親水性基を含有しな
い他のビニル単量体として、例えばハロゲン化ビ
ニル、ハロゲン化ビニリデン、アクリル酸または
メタクリル酸のアルキル、アラルキル、アリー
ル、アリルエステル、マレイン酸またはフマル酸
のアルキル、アラルキルエステル、アルキルビニ
ルエーテル、安息香酸ビニルエステル、置換また
は非置換スチレン、ジエン系化合物などが用いら
れる。これらの他のビニル単量体は、高価な含フ
ツ素ビニル単量体の増量目的で用いられ、ただし
撥水撥油性能、特に撥油性能を損わせることがあ
つてはならないので、共重合体中約90重量%以
下、好ましくは約80重量%以下の共重合割合で用
いられる。 共重合体中には、ドライクリーニング、ホーム
ウオツシング時などにおける撥水撥油剤の耐洗濯
性を高めるために、架橋性単量体、例えばN−メ
チロール(メタ)アクリルアミド、N−ブトキシ
メチロール(メタ)アクリルアミド、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、ジアセトンア
クリルアミド、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を、共重合体
中約0.01〜20重量%、好ましくは約0.5〜10重量
%程度共重合させる。 ランダム共重合反応は、含フツ素ビニル単量体
(約10〜100重量部、好ましくは約20〜80重量部)
他のビニル単量体(約90〜0重量部、好ましくは
約80〜20重量部)ならびに架橋性単量体、親水性
有機溶媒(約10〜10000重量部)および水(約90
〜20000重量部)を、コロイドミル、高速ホモジ
ナイザーなどを用いて十分に撹拌混合し、還流条
件下に十分窒素置換した後、アゾビスイソブチル
アミジン塩酸塩、過硫酸カリウム、過硫酸ナトリ
ウム、過硫酸アンモニウム、過酸化水素などの重
合開始剤を加え、もはや重合性単量体のGLC(ガ
スクロマトグラフイー)が消失する迄還流を継続
し、その時点を反応の終点とする。重合方法は、
こうした方法に限定される訳ではなく、通常の乳
化重合法の手法がそのまま採用される。 このランダム共重合反応の際、乳化剤は用いら
れず、特定の親水性有機溶媒の水溶液が反応の媒
体として用いられる。親水性有機溶媒としては、
メタノール、エタノール、n−プロパノール、イ
ソプロパノール、n−ブタノール、イソブタノー
ルなどの一価の低級アルコール、ジオキサン、テ
トラヒドロフランなどの環状エーテル、あるいは
アセトニトリル、ジメチルホルムアミド、ジメチ
ルアセトアミド、ジメチルスルホキシド、スルホ
ランなどの非プロトン性極性溶媒が、約5〜40
%、好ましくは約5〜20%の濃度で用いられる。 これらの親水性有機溶媒は、水と混和し得るこ
とは当然であるが、更にラジカル連鎖移動係数が
0.1×10-4以上、好ましくは0.2×104以上(60℃)
であることが望ましい。即ち、親水性有機溶媒化
合物は、連鎖移動により重合体鎖中に取り入れら
れることによつて、エマルジヨンの安定化に寄与
しているものと考えられ、また連鎖移動し難い溶
媒化合物の場合には親水性効果が大きければよ
く、あるいは親水性効果の小さい溶媒化合物でも
連鎖移動し易ければ好適に用いられる。かかる観
点からみて好ましい親水性有機溶媒は、メタノー
ル、イソプロパノール、アセトニトリルなどであ
る。 このようにして製造される本発明の撥水撥油剤
エマルジヨンは、乳化剤を不存在としている点に
おいて前記特許公開公報の撥水撥油剤エマルジヨ
ンと共通しているものの、後者においてはオキシ
アルキレン単位を9個以上有する親水性基含有重
合性化合物を共重合させ、それによつてエマルジ
ヨンを安定化させており、これは通常のソープフ
リー乳化重合法の手法そのものを撥水撥油剤共重
合体の製造に応用したにすぎず、それによつてエ
マルジヨンの安定化は達成されるものの、肝心の
撥水撥油性能、特に撥水性能の低下を招いている
のに対し、本発明の撥水撥油剤エマルジヨンにあ
つては、含フツ素ビニル単量体の共重合割合の比
較的少ない共重合体を用いても、それに本来求め
られている撥水撥油性能を殆んど損なうことな
く、安定なエマルジヨンを形成させている。 更に、当然のことながら、本発明に係るエマル
ジヨンにあつては乳化剤を用いていないため、廃
液などに対する特別の処理を不必要とさせる。こ
れに対し、例えば特公昭53−4159号公報などに記
載されているノニルフエニルエーテル/ポリエチ
レングリコール付加体のようなノニオン系界面活
性剤は、微生物分解がされ難く、公害処理対策が
重要となつてくる。また、本発明の撥水撥油剤エ
マルジヨンは、他の撥水撥油剤の如く泡立ちが著
しいというようなこともなく、末端ユーザー段階
での撥水撥油処理時の使用を非常に容易なものと
している。 本発明に係る共重合体エマルジヨンは、それを
水などで希釈して固型分濃度が約0.1〜1%の撥
水撥油剤濃度に調整した後、これをスプレー噴
霧、パツドマングル法(浸漬法)などにより、繊
維織物の原反加工に用いられ、その後乾燥(約80
〜120℃)および硬化(約120〜180℃)が行われ
る。 次に、実施例について本発明を説明する。 実施例 1 パーフルオロオクチルエチルアクリレート
50重量部 塩化ビニリデン 50 2−ヒドロキシエチルアクリレート 5 N−メチロールアクリルアミド 5 n−ドデシルメルカプタン 0.4 メタノール 53.2 水 422 上記各成分混合物をコロイドミルで十分に混合
撹拌し、次いで反応器内を十分窒素で置換した
後、重合開始剤としてアゾビスイソブチルアミジ
ン塩酸塩6.25重量部を加え、70〜80℃で8時間共
重合反応させた。乳白色乃至黄色のエマルジヨン
が得られ、これは3000rpm、10分間の遠心操作に
より、固型分濃度が18.8%から18.3%に低下する
のみであり、室温に6ケ月間放置した後も沈澱の
増加がなく、安定なエマルジヨン状態を形成して
いた。 このエマルジヨンを水で希釈して、固型分濃度
が0.5%の撥水撥油剤を調製し、この中に綿布
(布)、ポリエステル布(布)または綿
(65)/ポリエステル(35)混紡布(布)を浸
漬した。浸漬布について、80℃で15分間、次いで
170℃で3分間の熱処理を行ない、それについて
の撥水撥油性試験を行なつた。得られた試験結果
は、次の表1に示される。 表1 撥水性 布 100- 布 90+ 布 100 撥油性 布 130 布 150 布 130 〔撥水性試験〕 処理された布上に一滴の水を滴下し、5分間経
過後の状態を観察した。
The present invention relates to a method for producing a water and oil repellent emulsion. More specifically, the present invention relates to a method for producing a water and oil repellent emulsion that does not contain an emulsifier. Generally, water and oil repellent emulsions are manufactured using emulsifiers. Nonionic emulsifiers are used mainly for the following reasons. In other words, anionic and cationic emulsifiers tend to destabilize latex depending on the type of comonomer constituting the water/oil repellent copolymer, and in particular, cationic emulsifiers tend to destabilize the latex. Copolymers containing vinyl halides, vinylidene halides, etc. as comonomer components, which give good performance results, only give emulsions with poor stability. Furthermore, the presence of anionic emulsifiers significantly impairs water and oil repellency. Furthermore, these emulsifiers
Since it itself is ionic, it is not possible to freely adjust the composition with various fiber treatment agents. On the other hand, nonionic emulsifiers, such as polyethylene glycol alkyl phenol ether and polyethylene glycol alkyl ether, which are commonly used because of their excellent dispersibility, have poor biodegradability and are therefore Not only does it cause problems in wastewater treatment,
When vinyl halide, vinylidene halide, or the like is selected as a comonomer for a water- and oil-repellent copolymer, this biodegradation is promoted, and this is the cause of discoloration and discoloration of textiles. In order to avoid deterioration in performance of the water and oil repellent emulsion due to the presence of such an emulsifier, a polymerizable compound containing a perfluoroalkyl group having 8 or more carbon atoms and a polymerizable compound containing a hydrophilic group having 9 or more oxyalkylene units are included as structural units. An aqueous dispersion in which a copolymer is dispersed in an aqueous medium substantially without the use of an emulsifier has been proposed, and it has been reported in JP-A No. It is described in Publication No. 53-134786. However, this water and oil repellent agent shows a particular drop in water repellency, and even when a copolymer containing 60% by weight of a perfluoroalkyl group-containing polymerizable compound is used, its water repellency is 70%, which is good. At most
It is 80. As a result of various studies in search of a water and oil repellent emulsion that does not contain an emulsifier and has excellent water and oil repellency, the present inventors found that a vinyl monomer containing a fluoroalkyl group having 3 or more carbon atoms, Other vinyl monomers and crosslinking monomers that do not contain hydrophilic groups that can be copolymerized with this monomer are mixed with monohydric lower alcohols, cyclic ethers, or hydrophilic monomers that are aprotic polar solvents in the absence of emulsifiers. It has been discovered that a water and oil repellent emulsion that solves the above problems can be produced by random copolymerization in an aqueous organic solvent solution. Therefore, the present invention relates to a method for producing a water and oil repellent agent carried out in this manner. Examples of the vinyl monomer containing a fluoroalkyl group having 3 or more carbon atoms include the following compounds. However, in the formula, R is a divalent organic group, R' is a hydrogen atom or a methyl group,
R″ is a lower alkyl group, and n is 3 or more,
Generally it is an integer between 3 and 20. CH 2 =CR′COORC o F 2o+1 CH 2 =CR′COOCH 2 CH 2 C 6 F 13 CH 2 =CR′COOCH 2 CH 2 C 8 F 17 CH 2 =CR′COOCH 2 CH 2 C 10 F 21 CH 2 =CR′COOCH 2 CH 2 C 12 F 25 Other vinyl monomers that do not contain a hydrophilic group that can be copolymerized with this include, for example, vinyl halides, vinylidene halides, alkyl, aralkyl, aryl, allyl esters of acrylic acid or methacrylic acid, maleic acid, or fumaric acid. Alkyl acids, aralkyl esters, alkyl vinyl ethers, benzoic acid vinyl esters, substituted or unsubstituted styrenes, diene compounds, etc. are used. These other vinyl monomers are used to increase the amount of expensive fluorine-containing vinyl monomers, but they must not impair water and oil repellency, especially oil repellency, so they are commonly used. It is used in a copolymerization proportion of about 90% by weight or less, preferably about 80% by weight or less in the polymer. The copolymer contains crosslinkable monomers, such as N-methylol (meth)acrylamide and N-butoxymethylol ( meth)acrylamide, 2-hydroxyethyl (meth)acrylate, 2-hydroxypropyl (meth)acrylate, diacetone acrylamide, glycidyl (meth)acrylate, allyl glycidyl ether, etc., preferably in an amount of about 0.01 to 20% by weight in the copolymer. is copolymerized in an amount of about 0.5 to 10% by weight. In the random copolymerization reaction, a fluorine-containing vinyl monomer (about 10 to 100 parts by weight, preferably about 20 to 80 parts by weight)
Other vinyl monomers (approximately 90 to 0 parts by weight, preferably approximately 80 to 20 parts by weight) as well as crosslinking monomers, hydrophilic organic solvents (approximately 10 to 10,000 parts by weight) and water (approximately 90 to 0 parts by weight)
~20,000 parts by weight) were thoroughly stirred and mixed using a colloid mill, high-speed homogenizer, etc., and the mixture was thoroughly replaced with nitrogen under reflux conditions, followed by azobisisobutyramidine hydrochloride, potassium persulfate, sodium persulfate, ammonium persulfate, A polymerization initiator such as hydrogen peroxide is added, and reflux is continued until the polymerizable monomer GLC (gas chromatography) disappears, and that point is defined as the end point of the reaction. The polymerization method is
The method is not limited to these methods, and ordinary emulsion polymerization methods can be used as they are. During this random copolymerization reaction, no emulsifier is used, and an aqueous solution of a specific hydrophilic organic solvent is used as the reaction medium. As a hydrophilic organic solvent,
Monohydric lower alcohols such as methanol, ethanol, n-propanol, isopropanol, n-butanol, and isobutanol; cyclic ethers such as dioxane and tetrahydrofuran; or aprotic substances such as acetonitrile, dimethylformamide, dimethylacetamide, dimethylsulfoxide, and sulfolane. The polar solvent is approximately 5 to 40
%, preferably about 5-20%. These hydrophilic organic solvents are naturally miscible with water, but they also have a radical chain transfer coefficient.
0.1×10 -4 or more, preferably 0.2×10 4 or more (60℃)
It is desirable that In other words, hydrophilic organic solvent compounds are thought to contribute to stabilizing the emulsion by being incorporated into the polymer chain through chain transfer, and in the case of solvent compounds that are difficult to chain transfer, hydrophilic organic solvent compounds It is sufficient that the hydrophilic effect is large, or even a solvent compound with a small hydrophilic effect is preferably used as long as it is easy to chain transfer. From this point of view, preferred hydrophilic organic solvents include methanol, isopropanol, and acetonitrile. The water- and oil-repellent emulsion of the present invention produced in this manner is similar to the water- and oil-repellent emulsion of the above-mentioned patent publication in that no emulsifier is present, but in the latter, the oxyalkylene unit is 9 The emulsion is stabilized by copolymerizing a hydrophilic group-containing polymerizable compound having 1 or more hydrophilic groups, and the method of ordinary soap-free emulsion polymerization is applied to the production of water and oil repellent copolymers. Although this stabilizes the emulsion, it causes a decline in the essential water and oil repellency performance, especially the water repellency performance. Therefore, even if a copolymer with a relatively low copolymerization ratio of fluorine-containing vinyl monomer is used, a stable emulsion can be formed without almost impairing the water and oil repellency properties originally required of the copolymer. I'm letting you do it. Furthermore, as a matter of course, the emulsion according to the present invention does not use an emulsifier, so that no special treatment of waste liquid or the like is required. On the other hand, nonionic surfactants such as the nonyl phenyl ether/polyethylene glycol adduct described in Japanese Patent Publication No. 53-4159 are difficult to decompose by microorganisms, making it important to take measures against pollution. It's coming. In addition, the water and oil repellent emulsion of the present invention does not cause significant foaming unlike other water and oil repellents, making it extremely easy to use during water and oil repellent treatment at the end user stage. There is. The copolymer emulsion according to the present invention is prepared by diluting it with water or the like to adjust the solid content to a water and oil repellent concentration of about 0.1 to 1%, and then applying it by spraying, pad mangle method (immersion method), etc. It is used in the processing of raw fiber fabrics, and then dried (approximately 80%
~120°C) and curing (approximately 120-180°C). Next, the present invention will be explained with reference to examples. Example 1 Perfluorooctylethyl acrylate
50 parts by weight Vinylidene chloride 50 2-hydroxyethyl acrylate 5 N-methylolacrylamide 5 n-dodecyl mercaptan 0.4 Methanol 53.2 Water 422 The above component mixture was thoroughly mixed and stirred in a colloid mill, and then the inside of the reactor was sufficiently purged with nitrogen. Thereafter, 6.25 parts by weight of azobisisobutyramidine hydrochloride was added as a polymerization initiator, and a copolymerization reaction was carried out at 70 to 80°C for 8 hours. A milky-white to yellow emulsion was obtained, and the solid concentration only decreased from 18.8% to 18.3% by centrifugation at 3000 rpm for 10 minutes, and no increase in precipitation occurred even after leaving it at room temperature for 6 months. A stable emulsion state was formed. This emulsion is diluted with water to prepare a water and oil repellent with a solid content concentration of 0.5%, and cotton cloth (cloth), polyester cloth (cloth) or cotton (65)/polyester (35) blended fabric is added to this emulsion. (cloth) was soaked. For soaked cloth, at 80℃ for 15 minutes, then
A heat treatment was performed at 170° C. for 3 minutes, and a water and oil repellency test was conducted on the product. The test results obtained are shown in Table 1 below. Table 1 Water repellency Cloth 100 - Cloth 90 + Cloth 100 Oil repellency Cloth 130 Cloth 150 Cloth 130 [Water repellency test] A drop of water was dropped on the treated cloth, and the condition was observed after 5 minutes.

〔撥油性試験〕[Oil repellency test]

処理された布上に一滴の試験液(次の表に示さ
れる特定割合の混合液)を滴下し、5分間経過後
の状態を観察する。滴下された試験液が布上に保
持されている場合には、更にn−ヘプタン含量の
多い試験液で試験し、逆に布上に保持されない場
合には、更にヌジヨール含有の多い試験液で試験
する。そして、布上に保持されるのに限界の試験
液を以つて、次表の撥油性評価に基いて評価す
る。なお、撥油性評価において、100%ヌジヨー
ルを保持する場合を50、100%ヌジヨールを保持
しない場合を0とする。
A drop of the test solution (mixed solution in a specific proportion as shown in the table below) is placed on the treated fabric and the condition is observed after 5 minutes have elapsed. If the dropped test solution is retained on the cloth, test with a test solution containing more n-heptane, and conversely, if it is not retained on the cloth, test with a test solution containing even more n-heptane. do. Then, using the test liquid that can be retained on the cloth at its limit, the oil repellency is evaluated based on the oil repellency evaluation shown in the table below. In the oil repellency evaluation, the case where 100% Nudyol is retained is 50, and the case where 100% Nudyol is not retained is 0.

【表】 実施例 2〜3 実施例1において、塩化ビニリデンの代りに、
次のビニル共単量体のの同量が用いられた。 (実施例2) ベンジルメタクリレート (実施例3) ステアリルメタクリレート 実施例 4 実施例2において、パーフルオルオクチルエチ
ルアクリレートが75重量部、ベンジルメタクリレ
ートが25重量部用いられ、また2−ヒドロキシエ
チルアクリレートおよびN−メチロールアクリル
アミドの代りにジアセトンアクリルアミドが5重
量部用いられた。 実施例 5 実施例5において、パーフルオルオクチルエチ
ルアクリレートとベンジルメタクリレートとの使
用量が交換された。 実施例 6 実施例2において、2−ヒドロキシエチルアク
リレートとN−メチロールアクリルアミドとがそ
れぞれ1重量部用いられた。 実施例 7 実施例6において、メタノールの代りにジオキ
サンの同量が用いられた。 実施例 8 実施例6において、ベンジルメタクリレートの
代りに塩化ビニリデンが、またメタノールの代り
にアセトニトリルがそれぞれ同量用いられた。 実施例 9〜11 実施例1において、塩化ビニリデンの使用量を
35重量部に変更し、その代りに塩化ビニルを15重
量部用いた。また、2−ヒドロキシエチルアクリ
レートおよびN−メチロールアクリルアミドの代
りにジアセトンアクリルアミドが5重量部用いら
れ、更にメタノールの代りに次の親水性有機溶媒
の同量が用いられた。 (実施例9) ジメチルホルムアミド (実施例10) ジメチルスルホキシド (実施例11) スルホラン 実施例 12〜13 実施例1において、メタノールの代りに次の親
水性有機溶媒の同量が用いられた。 (実施例12) イソプロパノール (実施例13) イソブタノール 比較例 1〜2 実施例1において、塩化ビニリデンの使用量を
35重量部に変更し、その代りに塩化ビニルを15重
量部用いると共に、メタノールの代りに次の親水
性有機溶媒の同量が用いられた。 (比較例1) エチルセロソルブ (比較例2) プロピレングリコール 以上の実施例2〜13および比較例1〜2で得ら
れたそれぞれのエマルジヨンについて、実施例1
と同様に、エマルジヨンの安定性および撥水撥油
性の評価をそれぞれ行なつた。得られた試験結果
は、次の表2に示される。
[Table] Examples 2 to 3 In Example 1, instead of vinylidene chloride,
Equal amounts of the following vinyl comonomers were used: (Example 2) Benzyl methacrylate (Example 3) Stearyl methacrylate Example 4 In Example 2, 75 parts by weight of perfluorooctylethyl acrylate and 25 parts by weight of benzyl methacrylate were used, and 2-hydroxyethyl acrylate and N - 5 parts by weight of diacetone acrylamide were used instead of methylol acrylamide. Example 5 In Example 5, the amounts of perfluorooctylethyl acrylate and benzyl methacrylate were exchanged. Example 6 In Example 2, 1 part by weight each of 2-hydroxyethyl acrylate and N-methylolacrylamide was used. Example 7 In Example 6, the same amount of dioxane was used instead of methanol. Example 8 In Example 6, the same amount of vinylidene chloride was used instead of benzyl methacrylate, and the same amount of acetonitrile was used instead of methanol. Examples 9 to 11 In Example 1, the amount of vinylidene chloride used was
The amount was changed to 35 parts by weight, and 15 parts by weight of vinyl chloride was used instead. Furthermore, 5 parts by weight of diacetone acrylamide was used in place of 2-hydroxyethyl acrylate and N-methylol acrylamide, and the same amount of the following hydrophilic organic solvent was used in place of methanol. Example 9 Dimethylformamide (Example 10) Dimethyl sulfoxide (Example 11) Sulfolane Examples 12-13 In Example 1, methanol was replaced with the same amount of the following hydrophilic organic solvents. (Example 12) Isopropanol (Example 13) Isobutanol Comparative Examples 1-2 In Example 1, the amount of vinylidene chloride used was
35 parts by weight, 15 parts by weight of vinyl chloride was used instead, and the same amount of the following hydrophilic organic solvent was used instead of methanol. (Comparative example 1) Ethyl cellosolve (Comparative example 2) Propylene glycol For each emulsion obtained in Examples 2 to 13 and Comparative examples 1 to 2 above, Example 1
Similarly, the stability and water and oil repellency of the emulsion were evaluated. The test results obtained are shown in Table 2 below.

【表】 比較例 3 実施例1において、メタノールの代りにアセト
ンの同量が用いられた。重合反応中に生成共重合
体が沈澱し、安定なエマルジヨンを形成し得なか
つた。
Table Comparative Example 3 In Example 1, the same amount of acetone was used instead of methanol. During the polymerization reaction, the resulting copolymer precipitated, making it impossible to form a stable emulsion.

Claims (1)

【特許請求の範囲】[Claims] 1 炭素数3以上のフルオロアルキル基を含有す
るビニル単量体、これと共重合可能な親水性基を
含有しない他のビニル単量体および架橋性単量体
を、乳化剤の不存在下に、一価の低級アルコー
ル、環状エーテルまたは非プロトン性極性溶媒で
ある親水性有機溶媒水溶液中でランダム共重合さ
せることを特徴とする撥水撥油剤エマルジヨンの
製造法。
1 A vinyl monomer containing a fluoroalkyl group having 3 or more carbon atoms, another vinyl monomer that does not contain a hydrophilic group copolymerizable with this, and a crosslinkable monomer in the absence of an emulsifier, A method for producing a water and oil repellent emulsion, which comprises random copolymerization in an aqueous solution of a hydrophilic organic solvent such as a monovalent lower alcohol, a cyclic ether, or an aprotic polar solvent.
JP9378483A 1983-05-27 1983-05-27 Preparation of water-and oil-repellent emulsion Granted JPS59219380A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9378483A JPS59219380A (en) 1983-05-27 1983-05-27 Preparation of water-and oil-repellent emulsion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9378483A JPS59219380A (en) 1983-05-27 1983-05-27 Preparation of water-and oil-repellent emulsion

Publications (2)

Publication Number Publication Date
JPS59219380A JPS59219380A (en) 1984-12-10
JPS647634B2 true JPS647634B2 (en) 1989-02-09

Family

ID=14092034

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9378483A Granted JPS59219380A (en) 1983-05-27 1983-05-27 Preparation of water-and oil-repellent emulsion

Country Status (1)

Country Link
JP (1) JPS59219380A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3399107B2 (en) * 1994-09-05 2003-04-21 ダイキン工業株式会社 Antifouling agent composition having water and oil repellency
US6353051B1 (en) 1999-03-10 2002-03-05 E. I. Du Pont De Nemours And Company Top coating for synthetic leathers
JP5295176B2 (en) * 2010-05-26 2013-09-18 東洋インキScホールディングス株式会社 Method for producing composition for light scattering film, and light scattering film using the same

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3062765A (en) * 1957-04-03 1962-11-06 Minnesota Mining & Mfg Emulsion polymerization of water insoluble ethylenic monomers
US3102103A (en) * 1957-08-09 1963-08-27 Minnesota Mining & Mfg Perfluoroalkyl acrylate polymers and process of producing a latex thereof
JPS53134786A (en) * 1977-04-28 1978-11-24 Asahi Glass Co Ltd Water-and oil-repelling agents having improved stain-removing properties
JPS609692B2 (en) * 1977-09-24 1985-03-12 株式会社資生堂 Make-up cosmetics
JPS54132694A (en) * 1978-04-07 1979-10-15 Asahi Glass Co Ltd Preparation of high-performance water- and oil-repellent
JPS5571779A (en) * 1978-11-22 1980-05-30 Daikin Ind Ltd Water- and oil-repellent aqueous dispersion composition
DE3048883A1 (en) * 1980-12-23 1982-07-15 Boehringer Mannheim Gmbh, 6800 Mannheim Hydrophilic latex particles prodn. by emulsion polymerisation - without added surfactant, useful as carriers for biological or immunological cpds.
JPS5859277A (en) * 1981-10-06 1983-04-08 Asahi Glass Co Ltd Water/oil repellent
JPS6150082A (en) * 1984-12-20 1986-03-12 Tokyo Keiki Co Ltd Information processing system

Also Published As

Publication number Publication date
JPS59219380A (en) 1984-12-10

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