JPS6036515A - Manufacture of vinyl chloride resin - Google Patents

Manufacture of vinyl chloride resin

Info

Publication number
JPS6036515A
JPS6036515A JP14520483A JP14520483A JPS6036515A JP S6036515 A JPS6036515 A JP S6036515A JP 14520483 A JP14520483 A JP 14520483A JP 14520483 A JP14520483 A JP 14520483A JP S6036515 A JPS6036515 A JP S6036515A
Authority
JP
Japan
Prior art keywords
vinyl chloride
sialyl
prepolymer
monomer
resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP14520483A
Other languages
Japanese (ja)
Inventor
Masayuki Hida
雅之 飛田
Kunio Nomoto
野本 国夫
Mitsunori Kawanami
光則 河南
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo 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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP14520483A priority Critical patent/JPS6036515A/en
Publication of JPS6036515A publication Critical patent/JPS6036515A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the titled resin with good delustered appearance, by dissolving diallyl phthalate prepolymer in vinyl chloride monomer or its mixture with another monomer copolymerizable with it followed by graft copolymerization. CONSTITUTION:The objective resin can be obtained by dissolving (A) a diallyl phthalate prepolymer (pref. with an average molecular weight 4,000-30,000) in (B) vinyl chloride monomer or its mixture with another monomer copolymerizable with it (e.g., ethylene) (preferably with a weight ratio (A)/(B) of 0.5-20/ 99.5-80 followed by graft copolymerization, pref. in the presence of radical polymerization initiator (e.g., azobisisobutylonitrile) through aqueous suspension process.

Description

【発明の詳細な説明】 本発明は、フタル酸ジアリルデレポリマーニ塩化ビニル
系単量体乞グラフト共重合させる新規な艶消性塩化ビニ
ル系樹脂の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a novel matte vinyl chloride resin by graft copolymerizing a diallyl phthalate polymer with a divinyl chloride monomer.

塩化ビニル樹脂は、硬質板、管、波板、異形品などの硬
質用途や、フィルム、シート、しず−1床材、ホース、
履物などの軟質用途に広く利用されているが、その使用
目的によって成形品表面に艶が無い風合いに優れるもの
が安来され7′)。
PVC resin is used for rigid applications such as hard plates, pipes, corrugated sheets, and irregularly shaped products, as well as for films, sheets, Shizu-1 flooring, hoses,
It is widely used for soft products such as footwear, but depending on the purpose of use, molded products with excellent texture and no gloss are produced.7')

従来力・ら、艶消性に優れる成形品を得るために種々の
方法が検討されている。例えば、通常の塩化ビニル樹脂
の成形加工時の樹脂温度を低(させる方法、炭酸カルシ
ウム、コロイダルシリカナトの無機充填材を添加する方
法、アクリル系樹脂、エチレン−酢酸ビニル系共重合体
などの樹脂を添加する方法などがあるが、後述するよう
にいずれの方法によっても満足する艶消効果は得られな
かった。例えば、成形加工時の樹脂温度を低くする方法
では、樹脂の混練、溶融が不十分なために望まれる成形
品の機械的性質を低下させたり、表面艶消性が不均一に
なったりした。無得充埴剤や、他の樹脂を添加する方法
も、添加Iが少ないと艶消効果が不十分で、一方、多量
に添加しても明待される良好な艶消性は発現しなかった
Conventionally, various methods have been studied to obtain molded products with excellent matte properties. For example, methods of lowering the resin temperature during molding of ordinary vinyl chloride resin, methods of adding inorganic fillers such as calcium carbonate and colloidal silica, methods of adding resins such as acrylic resins, ethylene-vinyl acetate copolymers, etc. However, as described below, none of these methods yielded a satisfactory matting effect. For example, in the method of lowering the resin temperature during molding, the kneading and melting of the resin is not sufficient. Due to insufficient additive I, the desired mechanical properties of the molded product deteriorated and the surface matteness became uneven. The matting effect was insufficient, and even when a large amount was added, the expected good matting properties were not achieved.

一方、特公昭35−7590号公報、特公昭46−13
985号公報などに記載の塩化ビニル単量体と、マレイ
ン酸シアリル単一ボ:体及び、フマル酸シアリル単量体
の共重合体や特公昭38−1494号公報に記載の塩化
ビニル単量体と、フタル酸シアリル単一4体との共重合
体は、塩化ビニル単軟体と共重合可能なシアリルエステ
ル単量体との共重合体で、シアリルエステル単量体濃度
及び重合条件により分岐構造または溶剤に不溶な架構構
造を生成し、その成形加工品は、塩化ビニル単独重合体
と比較し、ある程度、表面艶消性が良好になる。
On the other hand, Special Publication No. 35-7590, Special Publication No. 46-13
Copolymers of vinyl chloride monomers, single sialyl maleates, and sialyl fumarate monomers described in Japanese Patent Publication No. 38-1494, etc., and vinyl chloride monomers described in Japanese Patent Publication No. 38-1494. The copolymer of sialyl phthalate and sialyl phthalate monomer is a copolymer of monosoft vinyl chloride and a copolymerizable sialyl ester monomer, and can have a branched structure or a branched structure depending on the sialyl ester monomer concentration and polymerization conditions. It produces a framework structure that is insoluble in solvents, and the molded product has a somewhat better surface matte property than vinyl chloride homopolymer.

しかし、これらシアリルエステル単量体との共重合体は
、シアリルエステル単量体の濃度が大きいほど、成形品
の艶消性が良好になるものの、成形品の強度を向上させ
るために高温条件で成形すると、成形品の゛艶消性にム
ラが生じ、美感を損ねたり、溶剤不溶分が増大し、成形
加工性が極度に悪化するためシアリルエステル単;寸体
の濃度は比較的低濃度に制限されていた。これらの現象
は、シアリルエステル単量体に限らず、エチレングリコ
ールジメタクリレート、トリアリルトリメリテート、ト
リアリルシアヌレートなどの単量体に共通のものであっ
た。
However, although copolymers with these sialyl ester monomers have a higher concentration of sialyl ester monomers, the matte properties of the molded products become better, but in order to improve the strength of the molded products, they cannot be used under high temperature conditions. When molded, the matteness of the molded product becomes uneven, impairing its aesthetic appearance, and the amount of solvent insoluble matter increases, resulting in extremely poor molding processability. It was restricted. These phenomena were common not only to sialyl ester monomers but also to monomers such as ethylene glycol dimethacrylate, triallyl trimellitate, and triallyl cyanurate.

また、特開昭56−79141号公報、特開昭57−1
0636号公報に記載の1分子中に塩化ビニル単量体と
共重合可能な少なくとも2個のエチレン性二重結合を有
するオリゴマー、例えばポリエチレングリコールゾメタ
クリレー)、1.2−ポリブタジエンなどと塩化ビニル
単量体との共重合によっても高温成形条件下での良好な
卵油性は得られないばかりか、フィッシュアイが生成り
Also, JP-A-56-79141, JP-A-57-1
Oligomers having at least two ethylenic double bonds in one molecule that are copolymerizable with vinyl chloride monomers, such as polyethylene glycol methacrylate), 1,2-polybutadiene, etc., and vinyl chloride described in Japanese Patent No. 0636 Copolymerization with monomers not only does not provide good egg oil properties under high-temperature molding conditions, but also produces fish eyes.

やすい欠点を有していた。It had some drawbacks.

本発明者らは、以上の種々の欠点を改良するために、鋭
意研究を重ねた結果、耐熱性に侵れる芳香族エステル結
合な主鎖に含有するフタル酸シアリルプレポリマーに、
塩化ビニル単月体、又は塩化ビニル単量体と共重合可能
な単量体をグラフト共重合させる艶消性塩化ビニル樹脂
の奥遣方法ケ見出した。
In order to improve the various drawbacks mentioned above, the present inventors have conducted intensive research and found that a sialyl phthalate prepolymer containing aromatic ester bonds in the main chain, which impairs heat resistance,
We have discovered a method for producing a matte vinyl chloride resin by graft copolymerizing vinyl chloride monomers or monomers copolymerizable with vinyl chloride monomers.

すなわち、本発明は、フタル酸ゾアリルデレポリマービ
、塩化ビニル単量体と、塩化ビニル単量体と共重合可能
な単量体との混合物に溶解させた後、ラソカル重合開始
剤を添加してグラフト共重合することビ特徴とする艶消
性塩化ビニル系樹脂の製造方法である。
That is, in the present invention, after dissolving a zoallyl phthalate polymer vinyl in a mixture of a vinyl chloride monomer and a monomer copolymerizable with the vinyl chloride monomer, a lasocal polymerization initiator is added. This is a method for producing a matte vinyl chloride resin, which is characterized by graft copolymerization.

以下、本発明についてさらに詳しく説明する。The present invention will be explained in more detail below.

本発明で使用するフタル酸ゾ“アリルプレポリマーを構
成する単位は、通常の7タル酸シアリル樹脂と同様で、
オルソフタル酸シアリル、イソフタル酸シアリルより選
ばiする少なくとも1種の単量体が挙げられる。このほ
かゾアリルクロレンデートもフタル酸シアリルと同様に
使用しうる。プレポリマー製造方法は、特公昭35−1
6035号公報、特公昭38−10344号公報などに
記載されている周知の方法でよく特に限定するものでは
ない。プレポリマーの平均分子量は、小さすぎるど、プ
レポリマー使用の特徴である高濃度添加と、高温艶消性
がやや劣り、太きすぎると、塩化ビニル単−叶体、又は
塩化ビニル単量体と共重合町tiEな単量体に対する溶
解性が低下し、重合系が不均一、不安定になるために、
4,000〜30.[100が好適である。
The units constituting the zoallyl phthalate prepolymer used in the present invention are the same as those of ordinary sialyl heptathalate resin,
At least one monomer selected from sialyl orthophthalate and sialyl isophthalate may be used. In addition, zoallyl chlorendate can also be used in the same manner as sialyl phthalate. The prepolymer manufacturing method is described in Japanese Patent Publication No. 35-1
Well-known methods described in Japanese Patent Publication No. 6035, Japanese Patent Publication No. 38-10344, etc. may be used, and there are no particular limitations. The average molecular weight of the prepolymer is too small, but the high-concentration addition that is characteristic of using a prepolymer and the high-temperature matting properties are slightly inferior. Because the solubility of copolymerized monomers decreases and the polymerization system becomes non-uniform and unstable,
4,000-30. [100 is preferred.

また、本発明で、上記フタル酸シアリルプレポリマーに
グラフト共重合させる塩化ビニル単量体又は塩化ビニル
単量体と共重合可能な弔団体の、塩化ビニル単量体と共
重合0T能な狛清体としてはエチレン、プロピレンなど
の、α−オレフィン入自、酢酸ビニル、ステアリン酸ビ
ニルなどのビニルエステル類、メチルビニルエーテル、
ラウリルビニルエーテルナトのビニルエーテル類、アク
リル酸メチル、メタクリル酸メチルなどのアクリル)t
Q、およびメタクリル酸のエステル類、メタクリルアミ
ド、アクリロニトリ ルなどのアミド、ニトリル類、ス
チレン、α−メチルスチレンなどのスチレン類、および
少量のフタル酸シアリル、エチレングリコールジメタク
リレートなどの多官能性単量体や、少量のポリエチレン
グリコールジメタクリレート、1,2−ポリブタジエン
などのオリゴ1−を含むものであり、幹ポリマーである
フタル酸シアリルプレポリマーの溶解性を損ねることの
ない種類、添〃D址であれば併用しても差し支えない。
In addition, in the present invention, the vinyl chloride monomer to be graft copolymerized with the sialyl phthalate prepolymer or the mourning group copolymerizable with the vinyl chloride monomer has a 0T ability to copolymerize with the vinyl chloride monomer. The bodies include α-olefins such as ethylene and propylene, vinyl esters such as vinyl acetate and vinyl stearate, methyl vinyl ether,
Vinyl ethers such as lauryl vinyl ether, acrylics such as methyl acrylate and methyl methacrylate)
Q, and esters of methacrylic acid, amides such as methacrylamide and acrylonitrile, nitriles, styrenes such as styrene and α-methylstyrene, and small amounts of polyfunctional monomers such as sialyl phthalate and ethylene glycol dimethacrylate. It contains a small amount of oligo 1- such as polyethylene glycol dimethacrylate and 1,2-polybutadiene, and does not impair the solubility of the sialyl phthalate prepolymer, which is the backbone polymer. There is no problem in using them together if they are available.

フタル(9)シアリルプレポリマーと塩化ビニル単量体
又はこれと共重合可能な単量体との仕込み割合は電鍍で
0.5〜2U対99,5〜80が好ましい。
The ratio of the phthal(9) sialyl prepolymer to the vinyl chloride monomer or a monomer copolymerizable therewith is preferably 0.5 to 2 U to 99.5 to 80 by electroplating.

本発明の;製造方法は、フタル酸シアリルプレポリマー
ン、上述の塩化ビニル単量体、又は塩化ビニル単量体ど
共重合可能な単量体との混合物に、溶解さぜた後に、ラ
ジカル重合開始剤を作用させることケ特徴とし、その取
合方法は塊状重合、懸濁重合、乳化重合、溶液重合、い
ずれの方法でも採用しうるが、なh・でも、重合温度の
調節、制御、脱水、ろ過などの操作が、工業的゛にも簡
便な懸濁重合が好ましい。以下、水性)(題濁重fKつ
いてさらに詳しく説明する。
The production method of the present invention involves dissolving the sialyl phthalate prepolymer, the above-mentioned vinyl chloride monomer, or a mixture with a copolymerizable monomer such as vinyl chloride monomer, followed by radical polymerization. It is characterized by the action of an initiator, and the polymerization method can be any of bulk polymerization, suspension polymerization, emulsion polymerization, and solution polymerization. Suspension polymerization is preferred because operations such as filtration and filtration are industrially easy. Hereinafter, the aqueous (water-based) (dark weight fK) will be explained in more detail.

懸濁安定剤として(・ま、塩化ビニル樹脂の懸濁重合に
通常使用される物質であれば良く、例えば、部分ケン化
ポリビニルアルコール、アルキルセルロース、ポリエチ
レングリコールの脂肪酸エステルなどを用いれば良い。
As the suspension stabilizer, any substance that is normally used for suspension polymerization of vinyl chloride resin may be used, such as partially saponified polyvinyl alcohol, alkyl cellulose, fatty acid ester of polyethylene glycol, etc.

フタル酸シアリルプレポリマーの溶解方法は特に限定し
ないが、重会缶に、純水、懸濁安定剤、フタル酸シアリ
ルプレポリマーなどを仕込み、脱気後、塩化ビニル単量
体を仕込み、30〜7 [) ”C程度の温度で、1な
いし2時間程度かくはんして、フタル酸シアリルプレポ
リマ〜酊溶解させる方法が良い。
The method for dissolving the sialyl phthalate prepolymer is not particularly limited, but pure water, suspension stabilizer, sialyl phthalate prepolymer, etc. are charged into a superimposed can, and after degassing, vinyl chloride monomer is charged, 7 [) A good method is to dissolve the sialyl phthalate prepolymer by stirring at a temperature of approximately 1 to 2 hours.

ラジカル重合開始剤は、油溶性の一ア・戸ピンイソブチ
ロニド リルなどのアゾ化合物ゾ、2エチルヘキシル、
パーオキシシカ−ボネートなどの角機禍酸化物など乞使
用し、7タル酸シアリルプレポリマーを塩化ビニル単量
体又は塩化ビニルjF吊体ど共重合可能な単量体に汀解
した後に、添加する。
Radical polymerization initiators include oil-soluble azo compounds such as isobutyronidrile, 2-ethylhexyl,
It is added after the sialyl heptatarate prepolymer is dissolved into a copolymerizable monomer such as vinyl chloride monomer or vinyl chloride jF suspension by using a oxidized oxide such as peroxycarbonate.

添加方法は、後添槽を用いて均圧法でも窒メソガス圧入
法でもかまわない。
The addition method may be a pressure equalization method or a nitrogen mesogas injection method using a post-addition tank.

以下、実施例及び比較例をあげて本発明を具体的に説明
するが、これらによって本発明は限定さ′hるものでは
ブよい。
The present invention will be specifically explained below with reference to Examples and Comparative Examples, but the present invention should not be limited by these.

実施例1 内容積6007のステンレス製オートクレーブに、懸濁
安定剤としてり′ン化度80モル係、平均屯合度240
0の部分ケン化ボリビニルアルニf −ル54 (、!
i’l、平均分子量10000.ヨウ素価どす0の7タ
ル酸シアリルプレポリマー2.4 (kl?) 、純水
18 D (kg) ”、を仕込み、オートクレープケ
真空にした後、塩化ビニル単量体57.6 Ckg) 
’&加え、攪拌しながら、55°Cで2時間、フタル酸
シアリルプレポリマーを浴1仔、懸濁させた。ラジカル
重合開始剤として、シー2エチルへキシルバーオキシゾ
カーポネート15 (g)?添加し、55℃で約12時
間取合した。未反応塩化ビニル単量体を回収し、スラリ
ー?常法により脱水、乾燥後、収Jよは51.0 (k
g)であった。得られた塩化ビニル系樹脂の≧゛IT−
価乞表に示す。
Example 1 In a stainless steel autoclave with an internal volume of 6007, a suspension stabilizer was added with a chlorination degree of 80 molar and an average concentration of 240.
Partially saponified polyvinyl albinol 54 (,!
i'l, average molecular weight 10000. After charging 2.4 (kl?) of sialyl 7-talate prepolymer with an iodine value of 0 and 18 D (kg) of pure water and evacuating it in an autoclave, 57.6 Ckg of vinyl chloride monomer was added.
'& was added and the sialyl phthalate prepolymer was suspended in one bath at 55°C for 2 hours with stirring. As a radical polymerization initiator, C-2-ethylhexyl silver oxyzocarbonate 15 (g)? The mixture was added and combined for about 12 hours at 55°C. Collect unreacted vinyl chloride monomer and make slurry? After dehydration and drying in a conventional manner, the yield was 51.0 (k
g). ≧゛IT− of the obtained vinyl chloride resin
Shown in the price list.

本発明の製造法で得られる艶消性塩化ビニル系樹脂は、
区好な表面艶消性が一要求される硬質板、管、波板、異
形品などの硬質成形品や、フィルム、しず−、床材、ホ
ース、高級電線被覆などの軟質成形品などに利用できろ
。また特に、高温成形条件ゲ必侠とする樹脂との共押出
成形品で表面艶消性が望まれる用途に好ましく利用でき
る。
The matte vinyl chloride resin obtained by the production method of the present invention is
For hard molded products such as hard plates, pipes, corrugated sheets, and irregularly shaped products that require a good surface matte property, and for soft molded products such as films, drips, flooring materials, hoses, and high-grade electric wire coatings. You can use it. In particular, it can be preferably used in applications where surface matte properties are desired in coextrusion molded products with resins that require favorable molding conditions at high temperatures.

実施例2〜5、比較例1.2 所定の平均分子量のフタル酸シアリルプレポリマー乞所
定時間で溶解し、実施例1ど同様に塩ffsビニル系樹
脂乞得た。(平均分子i仕7011 Oのフタル酸シア
リルのヨウ素価は85)。
Examples 2 to 5, Comparative Example 1.2 A sialyl phthalate prepolymer having a predetermined average molecular weight was dissolved in a predetermined time to obtain a salt ffs vinyl resin in the same manner as in Example 1. (The iodine value of sialyl phthalate with an average molecular i specification of 7011 O is 85).

比較例6 フタル1波シアリルプレポリマ=を使用しない以外は実
施例1と同様に行なった。
Comparative Example 6 The same procedure as in Example 1 was carried out except that the 1-wave phthalic sialyl prepolymer was not used.

実施例6 実施例1に於て塩化ビニル単量体57.6 (kq)の
代りに塩化ビニル重量体56.4に9及び酢酸ビニル単
hi一体1.2 (kg)を用いた以外は同様に太梅し
た。
Example 6 Same as in Example 1 except that vinyl chloride weight 56.4 to 9 and vinyl acetate monomer 1.2 (kg) were used instead of vinyl chloride monomer 57.6 (kq). It was fat plum.

比較1+ll 4 実施例1に於てフタル酸ゾアリルプ゛レポリマーの代り
にフタル酸シアリル単漣体な用いた以外は同様に実施し
た、 比較例5〜6 比較例60重合体に、フタル酸ゾアリルデレボ′リマー
を5X7(比較例5)、及び10kl?(比較例6)そ
れぞれ配合時にブレンドした。
Comparison 1+ll 4 The same procedure as in Example 1 was carried out except that sialyl phthalate monomer was used instead of the zoallyl phthalate prepolymer. Comparative Examples 5 to 6 Comparative Example 60 Polymer was added with sialyl phthalate 5×7 (Comparative Example 5), and 10 kl? (Comparative Example 6) Each was blended at the time of compounding.

実施例及び比較例で得られた塩化ビニル系樹脂の測定法
は次によった。
The vinyl chloride resins obtained in Examples and Comparative Examples were measured as follows.

(11THF不溶分(妬) 塩化ビニル糸樹脂2(g)を梢秤し、500 (mi)
のガラスビーカーにTHF、(テトラヒドロフラン)、
3 D Ot、91とともに投入し室温で約60時間放
置後、フィルターにてろ過し、不浴分乞取出し、風乾後
、年11秤、W (、!91する。THF不溶分(%)
は次式より算出した。
(11 THF-insoluble content) Weighed 2 (g) of vinyl chloride thread resin, 500 (mi)
THF, (tetrahydrofuran), in a glass beaker.
3 Added together with Ot, 91 and left at room temperature for about 60 hours, filtered through a filter, took out the unbathed portion, air-dried, weighed 11, W (,!91. THF insoluble content (%)
was calculated using the following formula.

THF不溶分(%l= −X100 塩化ビニル系樹脂50 (,91に、DOP (シー2
〜エチルヘキシルフタレート) 25(、V+、バリウ
ム、亜鉛脂肪酸塩複合安定剤1.5t、91 重質炭酸
カルシウム10(gl カーボンブラック0.5Fg+
を加えたトライブレンド物乞、表面温度1500 (ま
たは180”(1)、ロール間隙0.3朋の2本ロール
に投入し、粉末がシート状にロールに巻付いて力)ら5
分間、混練を続は取出した。取出したロールシートの表
面艶消性を目視観察により次の基準で評価した。
THF insoluble matter (%l= -X100 vinyl chloride resin 50 (,91, DOP (C2
~ethylhexyl phthalate) 25 (, V+, barium, zinc fatty acid salt composite stabilizer 1.5t, 91 heavy calcium carbonate 10 (gl carbon black 0.5Fg+
Tri-blend beggar with a surface temperature of 1500 (or 180" (1), rolled into two rolls with a roll gap of 0.3, the powder is wrapped around the rolls in a sheet form and the force is 5.
After kneading for a minute, the mixture was taken out. The surface matteness of the rolled sheet taken out was evaluated by visual observation according to the following criteria.

・艶消性が良好−−−−−○ ・艶消性に少しムラがあろ−−−−−△0艶が出ている
一−−−−x (2)のロール表面温度150”Cで約5分間混、伸し
たロールシートの、100朋四方の正方形表面積当りに
残存するフィッシュ−アイ、¥数え、次の基準で評価し
た。
・Good matting properties---○ ・Slightly uneven matting properties---△0 Glossy---x (2) Roll surface temperature of 150"C The fish eyes remaining per 100 square square surface area of the roll sheet mixed and stretched for about 5 minutes were counted and evaluated based on the following criteria.

・ 201固未満−−−−−〇 020〜1000個−一一一−△ 01[]00個より多い一−−−−x 表によると、フンル酸ゾアリルフ0し7)vリマーを添
加しない比較例3、および、フタル酸ゾアリルデレポリ
マーンブレンドした比較例5.6は150’01180
’Oいずれの艶消性も不良で7+;、る。
・Less than 201 solids---〇020~1000 pieces-111-△01[]More than 00 pieces----x According to the table, zoarylph fururate is 0 and 7) Comparison without adding vrimer Example 3 and Comparative Example 5.6, which is a blend of zoallyl phthalate derepolymer, is 150'01180
'O Both matte properties were poor at 7+;

また、フタル酸ジアリルプレポリマーの溶濱が不十分な
比較例、1.2はフィッシュ・アイが多(、。
In addition, Comparative Example 1.2, in which the diallyl phthalate prepolymer had insufficient melt edge, had many fish eyes.

フタル酸シアリル単量体との共重合体である比中−)例
4はロールシートが成形できなかった。
In Example 4, which is a copolymer with sialyl phthalate monomer, a roll sheet could not be formed.

これに対し、本発明による実施例1〜6は、いずれも1
50℃、180℃艶消性が優れ、フィッシュ・アイも少
なく良好である。
On the other hand, Examples 1 to 6 according to the present invention all have 1
Excellent matting properties at 50°C and 180°C, with few fish eyes.

特許出願人 電気化学工業株式会社 手続補正書 ■、 事件の表示 昭和58年特許願第145204号 2 発明の名称 塩化ビニル系樹脂の製造方法 3、 補正をする者 事件との関係 特許出願人 住 所 東京都千代田区有楽町l]川」4番I号名 称
 (329)電気化学工業株式会社明細書の発明の詳細
な説明の欄 5、 補正の内容 ■)第8頁第7行の「アゾピッイソ」を「アブビスイソ
−1と訂正する。
Patent Applicant Denki Kagaku Kogyo Co., Ltd. Procedural Amendment ■, Indication of Case Patent Application No. 145204 of 1982 Title of Invention Process for Manufacturing Vinyl Chloride Resin 3, Person Making Amendment Relationship to Case Patent Applicant Address [Yurakucho, Chiyoda-ku, Tokyo] No. 4 I Name (329) Denki Kagaku Kogyo Co., Ltd. Column 5 of the detailed description of the invention in the specification, Contents of the amendment■) "Azopiiso" on page 8, line 7 is corrected as ``Abbis Iso-1.''

3)第10頁第4〜5行の1−フタル酸ジアリル」を[
フタル酸ジアリルプレポリマー」と訂正する。
3) Diallyl 1-phthalate” on page 10, lines 4-5 [
Diallyl phthalate prepolymer” is corrected.

4)第10頁第18〜20行を[比較例3の重合体5(
Hglに平均分子量7000のフタル酸ジアリルプレポ
リマーを2.5Fg+(比較例5)、及び5(gl(比
較例6)それぞれ、艶消性とフィノシアイ評価時に配合
した。」と訂正する。
4) Page 10, lines 18-20 [Polymer 5 of Comparative Example 3 (
2.5Fg+ (Comparative Example 5) and 5(gl (Comparative Example 6)) were blended with Hgl and diallyl phthalate prepolymer having an average molecular weight of 7000 at the time of evaluation of matteness and finocia, respectively.'' is corrected.

5)第11頁表の比較例5.6中1−*(ブレンド■、
重量部)」を削除する。
5) 1-* (Blend■,
Weight part)" is deleted.

6)第12頁第5行のrTHF、(テトラヒドロフラン
)」をr’THF(テトラヒドロフラン)」と訂正する
6) On page 12, line 5, "rTHF, (tetrahydrofuran)" is corrected to "r'THF (tetrahydrofuran)."

7)第12頁第5行の「150°」を「150°C」と
訂正する。
7) Correct "150°" in line 5 of page 12 to "150°C".

8)第13頁第2行の後に次の文章を加える。8) Add the following sentence after the second line of page 13.

[なお、比較例5.6では、比較例3の重合体50 (
glに同様の配合剤と、平均分子量7000のフタル酸
ジアリルプレポリマーをそれぞれ2.5 (g)及び5
(g)配合した。] 9)第13頁第19行の「比較例、1.2」を「比較例
1.2」と訂正する。
[In addition, in Comparative Example 5.6, the polymer 50 of Comparative Example 3 (
2.5 (g) and 5 (g) of diallyl phthalate prepolymer with an average molecular weight of 7000 and the same formulation as gl.
(g) Blended. ] 9) Correct "Comparative Example, 1.2" on page 13, line 19 to "Comparative Example 1.2."

Claims (3)

【特許請求の範囲】[Claims] (1) フタル酸シアリルプレポリマーを塩化ビニル単
肝体又は塩化ビニルと共重脅可能な単皺体との混合物に
溶解後、グラフト共重合させること乞特徴とする艶消性
に優れた塩化ビニル系樹脂の製造方法。
(1) Vinyl chloride with excellent matte properties, which is characterized by dissolving a sialyl phthalate prepolymer in a monopolymer of vinyl chloride or a mixture of a monopolymerizable monomer with vinyl chloride and then graft copolymerizing the prepolymer. Method for producing resin.
(2)グラフト共重合はラジカル重合開始剤存在下水性
懸濁重合である特許請求の範囲第1項記載の(社)油性
に優れた塩化ビニル系樹脂の製造方法。
(2) The method for producing a vinyl chloride resin with excellent oiliness according to claim 1, wherein the graft copolymerization is aqueous suspension polymerization in the presence of a radical polymerization initiator.
(3) フタル酸シアリルプレポリマーは平均分子量が
400’0〜30000である特許請求の範囲第1項記
載の艶消性に優れた塩化ビニル系樹脂の製造方法。
(3) The method for producing a vinyl chloride resin with excellent matte properties according to claim 1, wherein the sialyl phthalate prepolymer has an average molecular weight of 400'0 to 30,000.
JP14520483A 1983-08-09 1983-08-09 Manufacture of vinyl chloride resin Pending JPS6036515A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14520483A JPS6036515A (en) 1983-08-09 1983-08-09 Manufacture of vinyl chloride resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14520483A JPS6036515A (en) 1983-08-09 1983-08-09 Manufacture of vinyl chloride resin

Publications (1)

Publication Number Publication Date
JPS6036515A true JPS6036515A (en) 1985-02-25

Family

ID=15379809

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14520483A Pending JPS6036515A (en) 1983-08-09 1983-08-09 Manufacture of vinyl chloride resin

Country Status (1)

Country Link
JP (1) JPS6036515A (en)

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