JPS6212925B2 - - Google Patents

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Publication number
JPS6212925B2
JPS6212925B2 JP17895781A JP17895781A JPS6212925B2 JP S6212925 B2 JPS6212925 B2 JP S6212925B2 JP 17895781 A JP17895781 A JP 17895781A JP 17895781 A JP17895781 A JP 17895781A JP S6212925 B2 JPS6212925 B2 JP S6212925B2
Authority
JP
Japan
Prior art keywords
weight
monomer
polymerization
vinyl
acid
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
JP17895781A
Other languages
Japanese (ja)
Other versions
JPS5880311A (en
Inventor
Yasushi Isobe
Masami Iwasaki
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.)
Toagosei Co Ltd
Original Assignee
Toagosei Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toagosei Co Ltd filed Critical Toagosei Co Ltd
Priority to JP17895781A priority Critical patent/JPS5880311A/en
Publication of JPS5880311A publication Critical patent/JPS5880311A/en
Publication of JPS6212925B2 publication Critical patent/JPS6212925B2/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、紙、セロフアン、金属箔、プラスチ
ツクフイルム、繊維製品などの表面加工、又は含
浸加工においてヒートシール剤或いはバインダー
として有用で新規な合成樹脂の水分散体を製造す
る方法に関するものである。 一般に上記基材にヒートシール剤或いはバイン
ダーとして使用せられる合成樹脂分散体は、その
処理皮膜が耐ブロツキング性であること、基材に
対する接着性、耐水性、耐油性、耐熱性、作業
性、さらにはコスト的に優位なることが要求せら
れる。 しかして、塩化ビニル重合体は、耐水性、耐油
性、耐薬品性、機械的強度などに優れた処理被膜
を与えるけれども、造膜性に乏しく上記基材に対
する密着性が不良であり、さらにそれに帰因して
引裂強度が低下する欠点をもつている。又、酢酸
ビニル重合体は被膜形成能や、密着性が優れてい
るが、機械的強度や、耐水性、耐アルカリ性、耐
油性に劣るという欠点をもつている。 本発明者らは単独重合体としては上記の優れた
諸物性を有する、塩化ビニルと酢酸ビニルとの共
重合体について、ヒートシール剤或いはバインダ
ーとしての機能向上を鋭意検討した結果、本発明
を見出した。 即ち本発明は塩化ビニル単量体25〜95重量%、
酢酸ビニル単量体5〜70重量%、メタリルスルホ
ン酸又はアリルスルホン酸(以下(メタ)アリル
スルホン酸と総称する)のアルカリ金属塩0.1〜
5.0重量%およびその他のエチレン系不飽和単量
体0〜40重量%からなる単量体混合物を、該単量
体混合物100重量部に対し、分散剤としてケン化
度80モル%以上、平均重合度500〜2000の部分ケ
ン化ポリビニルアルコール0.1〜3.0重量部の存在
下に水中で共重合させることを特徴とする合成樹
脂分散体の製造法である。 ヒートシール剤或いはバインダーは、一般的に
は水性分散体としての使用が工業的には有利であ
るが、水性分散体の形態をとるには長時間放置し
たり、機械的又は化学的な若干の悪条件下でも容
易に固形物を遊離させ得ない特性を有している必
要がある。又他の配合物、例えば可塑性、顔料、
磁性体などの金属粉、或いは熱安定化剤との分散
が容易で、安定な混合物を得ることが出来なけれ
ばならない。 斯様な諸物性を付与させるのに塩化ビニル及び
酢酸ビニル単量体と共にこれらの共重合単量体と
して(メタ)アリルスルホン酸のアルカリ金属塩
が好適である。 この単量体は極性の大きいスルホン酸のアルカ
リ金属塩であつて、これを生成重合体中に存在さ
せることにより、本発明の効果が得られるものと
解される。 本発明において各単量体の使用量は塩化ビニル
単量体が25〜95重量%であり、酢酸ビニル単量体
が5〜70重量%であることが上述の塩化ビニル重
合体及び酢酸ビニル重合体の各特性を有効に発揮
させるには必要である。塩化ビニル単量体が25重
量%未満の場合は耐水性、耐油性、機械的強度の
よい被膜が得られず、95重量%を越えると合成樹
脂分散体の造膜性が乏しく、基材に対する密着性
が不良となる。また酢酸ビニル単量体が5重量%
未満の場合は造膜性や密着性が改善されず、70重
量%を越えると機械的強度、耐水性、耐油性が不
良となる。好ましい使用量は塩化ビニル単量体30
〜90重量%、酢酸ビニル単量体10〜65重量%であ
る。さらに(メタ)アリルスルホン酸のアルカリ
金属塩の使用量は0.1〜5.0重量%であることが必
要であり、0.3〜3.0重量%が好ましい。0.1重量%
未満の場合は、前記したその使用効果が認められ
ず、5.0重量%を越えると、重合速度及び重合度
の著しい低下がみられ好ましくない。 本発明の必須単量体である上記の3種類の単量
体以外の単量体として使用可能なエチレン系不飽
和単量体としては、製造する重合体又は重合体を
含む組成物の目的とする物性の調整の為、40重量
%以下の使用量で適宜使用される。一般的にはガ
ラス転移温度、溶解性パラメーター、架橋密度な
どの調整の為に下記の単量体を選ぶことが出来
る。 例えばアクリル酸エステルとして、アクリル酸
ブチル、アクリル酸2−エチルヘキシル、アクリ
ル酸エトキシエチル、アクリル酸メトキシプロピ
ル等が挙げられる。ビニルアルキルエーテルとし
ては、ペン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、セチルビニ
ルエーテルなどが挙げられる。 飽和脂肪酸のビニルエステルとしては、吉草酸
ビニルエステル、カプリル酸ビニルエステル、カ
プリン酸ビニルエステル、ラウン酸ビニルエステ
ルなどが挙げられる。又ハロゲンを含む単量体と
して、塩化ビニリデン、臭化ビニル、塩化メタア
リル、クロル酪酸ビニルなどが挙げられる。他の
官能基を与える単量体としては、アクリル酸、メ
タアクリル酸、メタアクリル酸グリシジルエステ
ル、アクリルアミド、N−メチロ−ルアクリルア
ミドなどが挙げられる。又反応性の大なる官能基
を有する単量体、例えば、アクリル酸、メタアク
リル酸、N−メチロ−ルアクリルアミドなどの使
用にあたつては、2.0重量%以下が好ましい。こ
れらの単量体は、使用量が多いと重合反応中、ゲ
ル分を生成し易いからである。 次にこれらの単量体を水中で共重合させるのに
必要な分散剤である部分ケン化ポリビニルアルコ
ールについて説明する。 この分散剤は、前述の(メタ)アリルスルホン
酸のアルカリ金属塩との同時使用により、良好な
重合系の分散状態を与える。即ち、通常の重合方
法では得られ難いとされている若干多孔質で1〜
数ミクロンの粒径をもつ分散された重合体を得る
ことが出来る。これにより可塑剤、熱安定化剤な
どの配合剤とのブレンド性が良好となる。 斯る目的を満足させるPVAの部分ケン化物
は、ケン化度80モル%以上、平均重合度500〜
2000であることが必要である。この条件を逸脱す
ると重合系の分散状態が著しく不安定となり好ま
しくない。 又、この分散剤の使用量は単量体混合物100重
量部に対して、0.1〜0.3重量部であることが必要
であり、0.2〜2.0重量部が好ましい。0.1重量部未
満の場合、粒径が著しく不均一であり、且つ0.1
ミクロン以下の微細粒子が生成し、生成分散体の
粘度変化が大となり、他方3.0重量部を越えると
重合反応系の粘度が上昇し、不安定な分散系を与
えることとなるので共に不適当である。 本発明においては、前述の各成分を所定量配合
し、これらを公知の重合方法により、水中下で共
重合させることにより、合成樹脂分散体が得られ
る。この際、他種の分散剤乃至は乳化剤を併用す
ることも勿論さしつかえない。例えば、アルキル
セルロース、ヒドロキシアルキルセルロース、ゼ
ラチンなどの分散剤、アルキルアリルスルホン酸
塩、アルキル硫酸塩、ポリオキシエチレンアルキ
ルアリルエーテル、ポリオキシエチレンアリール
硫酸塩、スルホコハク酸エステルアルカリ塩など
の乳化剤が適宜使用出来る。触媒としては、過硫
酸カリウム、過硫酸アンモニウム、過酸水化水素
などの水溶性化合物、過酸化ベンゾイル、アゾビ
スイソブチロニトリル、ジ−2エチルヘキシパー
オキシジカーボネート、過酸化ラウロイルなどの
油溶性化合物が重合方式に応じ選択して用いるこ
とが出来る。重合方式は乳化重合法又は懸濁重合
法が用いられる。その他の重合条件は常法に従つ
て行なうことができる。 このようにして得られた共重合体は水性分散体
として、種々の用途に応じたヒートシール剤或い
はバインダーとして用いられる。この場合特に可
塑剤、熱安定化剤とブレンドして用いる場合本方
法で得た合成樹脂分散体が有効である。ブレンド
法としては可塑剤など重合反応上差程支障をきた
さない化合物の場合は、予め、重合系に存在させ
て重合反応を為さしめる方法を採用すると好結果
をもたらす。斯る可塑剤としては、エポキシ化ダ
イズ油、エポキシ化アマニ油、ジブチルフタレー
ト、ジイソデシルフタレートなどが挙げられる。 本発明によれば塩化ビニル樹脂と酢酸ビニル樹
脂の各々の長所、即ちすぐれた機械的強度、耐水
性、耐油性、接着性、引裂強度及び或膜性などの
重要な特性を有する合成樹脂分散体が容易に得ら
れ、紙、セロフアン、金属箔、プラスチツクフイ
ルム、繊維製品などの基材に対するヒートシール
剤又はバインダーとして特に有用である。 次に本発明の実施例並びに比較例をあげ、さら
に具体的に説明する。 なお各例における物性試験は次の方法に従つ
た。 (1) ヒートシール強度 テトロン/木綿(65/35)の混紡布に重合体
若しくはそれを含む組成物を均一に固形分とし
て15〜20gr/m2で散布し、これに塩化ビニル軟
質レザーを合わせ、150℃×5Kg/cm2×10秒間
の条件でヒートシールし、幅20m/mの剥離強
度を測定した。 (2) 引裂強度 ヒートシール強度の測定の為に調製せられた
試験基材(厚さ0.8〜1.0m/m)に切口を入
れ、180゜で引裂いた場合の強度をみた。(値は
負荷重を厚さで除して求めた。) (3) 耐水性 ヒートシール強度の測定の為に調製せられた
試験基材を20℃純水中に3日間浸漬后、剥離強
度を測定し、同強度を浸漬前の強度で除し、保
持率を求めた。 (4) 最低成膜温度 熱傾斜式成膜形成温度測定試験機で水性分散
体から一様なフイルムを形成する最低温度を測
定した。 (5) 放置安定性 得られた水性分散体を40℃×2週間放置し、
ケーキ状固形物の遊離の有無を観察した。 実施例1〜7および比較例1〜3 5のステンレス製重合器に純水140重量部、
表1の単量体組成の条件下で全単量体として100
重量部、分散剤として部分ケン化PVAを、表1
の如く使用し、触媒として過硫酸カリウム0.4重
量部を添加して、常温にて、700rpmで30分間、
予備撹拌后、60℃×200rpm×20Hr乳化重合し固
形分40重量%の水性分散体を得た。 この水性分散体をブレードコーターで、基材に
塗布し、前記の各試験を実施した。
The present invention relates to a method for producing a novel aqueous dispersion of a synthetic resin useful as a heat sealing agent or binder in surface processing or impregnation processing of paper, cellophane, metal foil, plastic film, textile products, etc. Generally, the synthetic resin dispersion used as a heat sealant or binder for the above-mentioned substrates has the following characteristics: the treated film has blocking resistance, adhesion to the substrate, water resistance, oil resistance, heat resistance, workability, and is required to be advantageous in terms of cost. Although vinyl chloride polymers provide treated films with excellent water resistance, oil resistance, chemical resistance, and mechanical strength, they have poor film-forming properties and poor adhesion to the above-mentioned substrates. As a result, it has the disadvantage of reduced tear strength. Furthermore, although vinyl acetate polymers have excellent film-forming ability and adhesion, they have the drawbacks of poor mechanical strength, water resistance, alkali resistance, and oil resistance. The present inventors have intensively investigated ways to improve the functionality of a copolymer of vinyl chloride and vinyl acetate, which has the above-mentioned excellent physical properties as a homopolymer, as a heat sealing agent or binder, and have discovered the present invention. Ta. That is, the present invention contains 25 to 95% by weight of vinyl chloride monomer,
5 to 70% by weight of vinyl acetate monomer, 0.1 to 0.1 to alkali metal salt of methallylsulfonic acid or allylsulfonic acid (hereinafter collectively referred to as (meth)allylsulfonic acid)
A monomer mixture consisting of 5.0% by weight and 0 to 40% by weight of other ethylenically unsaturated monomers is added as a dispersant to 100 parts by weight of the monomer mixture, with a degree of saponification of 80 mol% or more, average polymerization. This is a method for producing a synthetic resin dispersion characterized by copolymerizing in water in the presence of 0.1 to 3.0 parts by weight of partially saponified polyvinyl alcohol having a degree of 500 to 2000. Generally, it is industrially advantageous to use heat sealants or binders in the form of aqueous dispersions; It must have the property of not being able to easily release solids even under adverse conditions. Also other formulations, such as plastics, pigments,
It must be possible to easily disperse the metal powder such as a magnetic material or a thermal stabilizer to obtain a stable mixture. In order to impart such physical properties, an alkali metal salt of (meth)allylsulfonic acid is suitable as a comonomer of these together with vinyl chloride and vinyl acetate monomers. This monomer is a highly polar alkali metal salt of sulfonic acid, and it is understood that the effects of the present invention can be obtained by allowing it to exist in the produced polymer. In the present invention, the amount of each monomer used is 25 to 95% by weight of vinyl chloride monomer and 5 to 70% by weight of vinyl acetate monomer. It is necessary to effectively exhibit each characteristic of merging. If the vinyl chloride monomer content is less than 25% by weight, a film with good water resistance, oil resistance, and mechanical strength cannot be obtained, and if it exceeds 95% by weight, the film forming properties of the synthetic resin dispersion are poor and Adhesion becomes poor. Also, vinyl acetate monomer is 5% by weight.
If it is less than 70% by weight, film forming properties and adhesion will not be improved, and if it exceeds 70% by weight, mechanical strength, water resistance, and oil resistance will be poor. The preferred amount used is vinyl chloride monomer 30
~90% by weight, vinyl acetate monomer 10-65% by weight. Further, the amount of the alkali metal salt of (meth)allylsulfonic acid used must be 0.1 to 5.0% by weight, preferably 0.3 to 3.0% by weight. 0.1% by weight
If it is less than 5.0% by weight, the above-mentioned effects of use will not be observed, and if it exceeds 5.0% by weight, the polymerization rate and degree of polymerization will be significantly lowered, which is not preferable. Ethylenically unsaturated monomers that can be used as monomers other than the above three types of monomers that are essential monomers of the present invention include It is used in an amount of 40% by weight or less to adjust the physical properties. Generally, the following monomers can be selected to adjust the glass transition temperature, solubility parameter, crosslink density, etc. Examples of acrylic esters include butyl acrylate, 2-ethylhexyl acrylate, ethoxyethyl acrylate, methoxypropyl acrylate, and the like. Examples of the vinyl alkyl ether include pentyl vinyl ether, octyl vinyl ether, lauryl vinyl ether, and cetyl vinyl ether. Examples of vinyl esters of saturated fatty acids include valeric acid vinyl ester, caprylic acid vinyl ester, capric acid vinyl ester, and lauric acid vinyl ester. Examples of monomers containing halogen include vinylidene chloride, vinyl bromide, methallyl chloride, vinyl chlorobutyrate, and the like. Examples of monomers providing other functional groups include acrylic acid, methacrylic acid, methacrylic acid glycidyl ester, acrylamide, and N-methylol acrylamide. Furthermore, when using monomers having highly reactive functional groups, such as acrylic acid, methacrylic acid, and N-methylol acrylamide, the amount is preferably 2.0% by weight or less. This is because if these monomers are used in large amounts, they tend to form gel components during the polymerization reaction. Next, partially saponified polyvinyl alcohol, which is a dispersant necessary for copolymerizing these monomers in water, will be explained. This dispersant provides a good dispersion state of the polymerization system when used simultaneously with the alkali metal salt of (meth)allylsulfonic acid mentioned above. In other words, it is a slightly porous material that is difficult to obtain with normal polymerization methods.
Dispersed polymers with particle sizes of several microns can be obtained. This improves blendability with compounding agents such as plasticizers and heat stabilizers. Partially saponified PVA that satisfies these purposes has a degree of saponification of 80 mol% or more and an average degree of polymerization of 500 or more.
Must be 2000. If this condition is exceeded, the dispersion state of the polymerization system becomes extremely unstable, which is not preferable. The amount of the dispersant used must be 0.1 to 0.3 parts by weight, preferably 0.2 to 2.0 parts by weight, based on 100 parts by weight of the monomer mixture. If it is less than 0.1 part by weight, the particle size is significantly non-uniform, and
Fine particles of micron size or less will be generated, and the viscosity of the resulting dispersion will change greatly. On the other hand, if it exceeds 3.0 parts by weight, the viscosity of the polymerization reaction system will increase, giving an unstable dispersion system, so both are unsuitable. be. In the present invention, a synthetic resin dispersion is obtained by blending predetermined amounts of each of the above-mentioned components and copolymerizing them in water using a known polymerization method. At this time, it is of course possible to use other types of dispersants or emulsifiers in combination. For example, dispersants such as alkyl cellulose, hydroxyalkyl cellulose, and gelatin, emulsifiers such as alkylaryl sulfonates, alkyl sulfates, polyoxyethylene alkyl allyl ethers, polyoxyethylene aryl sulfates, and alkali salts of sulfosuccinates are used as appropriate. I can do it. Examples of catalysts include water-soluble compounds such as potassium persulfate, ammonium persulfate, and hydrogen peroxide hydride, and oils such as benzoyl peroxide, azobisisobutyronitrile, di-2-ethylhexyperoxydicarbonate, and lauroyl peroxide. Soluble compounds can be selected and used depending on the polymerization method. As the polymerization method, emulsion polymerization method or suspension polymerization method is used. Other polymerization conditions can be carried out according to conventional methods. The copolymer thus obtained is used in the form of an aqueous dispersion as a heat sealing agent or a binder for various uses. In this case, the synthetic resin dispersion obtained by this method is particularly effective when blended with a plasticizer and a heat stabilizer. In the case of a blending method, in the case of a compound such as a plasticizer that does not cause much trouble in the polymerization reaction, good results can be obtained by employing a method in which the compound is made to exist in the polymerization system in advance and the polymerization reaction is carried out. Such plasticizers include epoxidized soybean oil, epoxidized linseed oil, dibutyl phthalate, diisodecyl phthalate, and the like. According to the present invention, a synthetic resin dispersion having the respective advantages of vinyl chloride resin and vinyl acetate resin, that is, important properties such as excellent mechanical strength, water resistance, oil resistance, adhesion, tear strength and filmability, is produced. is easily obtained and is particularly useful as a heat sealing agent or binder for substrates such as paper, cellophane, metal foil, plastic film, and textile products. Next, Examples and Comparative Examples of the present invention will be given and explained in more detail. In addition, the physical property test in each example was conducted according to the following method. (1) Heat sealing strength A polymer or a composition containing it is uniformly sprinkled on a Tetoron/cotton (65/35) blended fabric at a solid content of 15 to 20g/ m2 , and then PVC soft leather is added to this. , heat-sealed under the conditions of 150° C. x 5 Kg/cm 2 x 10 seconds, and the peel strength at a width of 20 m/m was measured. (2) Tear strength A cut was made in a test base material (thickness 0.8 to 1.0 m/m) prepared for measuring heat seal strength, and the strength was measured when it was torn at 180°. (The value was calculated by dividing the load by the thickness.) (3) Water resistance After immersing the test base material prepared for measuring heat seal strength in pure water at 20°C for 3 days, the peel strength was measured. was measured, and the same strength was divided by the strength before immersion to determine the retention rate. (4) Minimum film forming temperature The lowest temperature at which a uniform film was formed from the aqueous dispersion was measured using a thermal gradient film forming temperature measurement tester. (5) Storage stability The obtained aqueous dispersion was left at 40°C for 2 weeks.
The presence or absence of release of cake-like solid matter was observed. Examples 1 to 7 and Comparative Examples 1 to 3 140 parts by weight of pure water was added to the stainless steel polymerization vessel of 5.
100 as the total monomer under the conditions of the monomer composition in Table 1.
Parts by weight, partially saponified PVA as dispersant, Table 1
0.4 parts by weight of potassium persulfate was added as a catalyst, and the mixture was heated at room temperature at 700 rpm for 30 minutes.
After preliminary stirring, emulsion polymerization was carried out at 60° C. x 200 rpm x 20 hours to obtain an aqueous dispersion with a solid content of 40% by weight. This aqueous dispersion was applied to a substrate using a blade coater, and the above-mentioned tests were conducted.

【表】【table】

【表】 比較例 4及び5 単量体及び分散剤については、表2に示した条
件とし、その他は前記実施例1〜7および比較例
1〜3に記載された方法と同一条件により水性分
散体を得た。 この水性分散体について、前記の各試験を実施
した。 その結果を表2に示した。
[Table] Comparative Examples 4 and 5 Monomers and dispersants were used under the conditions shown in Table 2, and other conditions were the same as those described in Examples 1 to 7 and Comparative Examples 1 to 3. I got a body. The above-mentioned tests were conducted on this aqueous dispersion. The results are shown in Table 2.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 塩化ビニル単量体25〜95重量%、酢酸ビニル
単量体5〜70重量%、メタリルスルホン酸又はア
リルスルホン酸のアルカリ金属塩0.1〜5.0重量%
およびその他のエチレン系不飽和単量体0〜40重
量%からなる単量体混合物を、該単量体混合物
100重量部に対し、分散剤としてケン化度80モル
%以上、平均重合度500〜2000の部分ケン化ポリ
ビニルアルコール0.1〜3.0重量部の存在下に水中
で共重合させることを特徴とする合成樹脂分散体
の製造法。
1 Vinyl chloride monomer 25-95% by weight, vinyl acetate monomer 5-70% by weight, alkali metal salt of methallylsulfonic acid or allylsulfonic acid 0.1-5.0% by weight
A monomer mixture consisting of 0 to 40% by weight of other ethylenically unsaturated monomers is added to the monomer mixture.
A synthetic resin characterized by being copolymerized in water in the presence of 0.1 to 3.0 parts by weight of partially saponified polyvinyl alcohol having a degree of saponification of 80 mol% or more and an average degree of polymerization of 500 to 2000 as a dispersant per 100 parts by weight. Method for manufacturing dispersion.
JP17895781A 1981-11-10 1981-11-10 Production of synthetic resin dispersion Granted JPS5880311A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17895781A JPS5880311A (en) 1981-11-10 1981-11-10 Production of synthetic resin dispersion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17895781A JPS5880311A (en) 1981-11-10 1981-11-10 Production of synthetic resin dispersion

Publications (2)

Publication Number Publication Date
JPS5880311A JPS5880311A (en) 1983-05-14
JPS6212925B2 true JPS6212925B2 (en) 1987-03-23

Family

ID=16057612

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17895781A Granted JPS5880311A (en) 1981-11-10 1981-11-10 Production of synthetic resin dispersion

Country Status (1)

Country Link
JP (1) JPS5880311A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4767816A (en) * 1987-06-24 1988-08-30 Air Products And Chemicals, Inc. Polyvinyl alcohol-stabilized vinyl chloride-ethylene-hydroxyethyl acrylate copolymer emulsions having enhanced water and solvent resistant properties

Also Published As

Publication number Publication date
JPS5880311A (en) 1983-05-14

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