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JPS5836015B2 - resin composition - Google Patents
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JPS5836015B2 - resin composition - Google Patents

resin composition

Info

Publication number
JPS5836015B2
JPS5836015B2 JP14301580A JP14301580A JPS5836015B2 JP S5836015 B2 JPS5836015 B2 JP S5836015B2 JP 14301580 A JP14301580 A JP 14301580A JP 14301580 A JP14301580 A JP 14301580A JP S5836015 B2 JPS5836015 B2 JP S5836015B2
Authority
JP
Japan
Prior art keywords
weight
vinyl chloride
parts
graft copolymer
eva
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
JP14301580A
Other languages
Japanese (ja)
Other versions
JPS5767646A (en
Inventor
延男 森下
克巳 西崎
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.)
Tosoh Corp
Original Assignee
Toyo Soda Manufacturing 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 Toyo Soda Manufacturing Co Ltd filed Critical Toyo Soda Manufacturing Co Ltd
Priority to JP14301580A priority Critical patent/JPS5836015B2/en
Publication of JPS5767646A publication Critical patent/JPS5767646A/en
Publication of JPS5836015B2 publication Critical patent/JPS5836015B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明はすぐれた透明性を有する樹脂組或物に関する。[Detailed description of the invention] The present invention relates to a resin composite having excellent transparency.

さらに詳しくは、エチレンー酢酸ビニル共重合体(以下
、EVAと略す)の存在下に塩化ビニル七ノマーもしく
は塩化ビニルモノマーを主体とする七ノマー混合物を重
合させることにより製造される軟質塩化ビニル系グラフ
ト共重合体とフェノール樹脂からなる透明性にすぐれた
樹脂組成物に関する。
More specifically, the soft vinyl chloride graft copolymer is produced by polymerizing a vinyl chloride heptanomer or a heptanomer mixture mainly composed of vinyl chloride monomers in the presence of an ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVA). This invention relates to a resin composition with excellent transparency consisting of a polymer and a phenol resin.

従来、ポリ塩化ビニル(以下PVCと略す)の軟質分野
においては、可塑剤の揮発あるいは移行が問題となって
おり、無可塑軟質化を目的としてEVAとPVCのブレ
ンド、あるいは、EVA一、の塩化ビニルグラフトなど
が行われてきた。
Conventionally, in the field of soft polyvinyl chloride (hereinafter abbreviated as PVC), volatilization or migration of plasticizers has been a problem, and blends of EVA and PVC or chlorination of EVA and EVA have been used for the purpose of making plasticizers soft and non-plastic. Vinyl grafting has been done.

EVA塩化ビニルグラフト共重合体においてEVA含量
を漸次増加させるとグラフト共重合体は硬質から半硬質
へ、さら軟質タイプへと性質が移行することはよく知ら
れており、特公昭39−27876などの方法によると
EVA含量の多いグラフト共重合体を得ることができる
ことも公知である。
It is well known that when the EVA content of an EVA vinyl chloride graft copolymer is gradually increased, the properties of the graft copolymer change from hard to semi-hard to soft. It is also known that the process makes it possible to obtain graft copolymers with a high EVA content.

しかし、EVA含量を多くした、EVA一塩化ビニルグ
ラフト共重合体は、柔軟性は増すもののいくつかの問題
点が未だ解決されておらず、そのため、フタル酸エステ
ルなどで可塑化した軟質PVCを限られた分野でしか代
替するに到っていない。
However, although the EVA monochloride graft copolymer with a high EVA content has increased flexibility, some problems remain unsolved, and as a result, it is limited to soft PVC plasticized with phthalate esters. It has only reached the point where it can be replaced in the areas where it has been replaced.

特に透明性は、今迄、まぬがれることのできなかった欠
点であり、透明性が要求される用途には軟質EVA一塩
化ビニルグラフト共重合体を使用することができなかっ
た。
Transparency in particular has been an unavoidable drawback until now, and soft EVA-vinyl monochloride graft copolymers have not been able to be used in applications requiring transparency.

本発明は、軟質EVA一塩化ビニルグラフト共重合体の
欠点であった透明性の問題の簡単でかつ経済的な解決法
を提供することを目的とするものである。
The present invention aims to provide a simple and economical solution to the transparency problem that has been a drawback of flexible EVA vinyl monochloride graft copolymers.

この目的を達戊するために、本発明ではエチレン戒分が
35〜75重量%であるEVA15〜70重量部の存在
下に、塩化ビニルモノマーもしくは塩化ビニルモノマー
を主体とするモノマー混合物30〜85重量部を重合さ
せることにより得られる軟質塩化ビニル系グラフト共重
合体100重量部にフェノール樹脂0,5〜50重量部
を配合することを行ないすぐれた透明性を有する軟質塩
化ビニル系グラフト共重合体を得ることができた。
To achieve this objective, in the present invention, 30 to 85 parts by weight of vinyl chloride monomer or a monomer mixture mainly composed of vinyl chloride monomer is added in the presence of 15 to 70 parts by weight of EVA having an ethylene content of 35 to 75% by weight. A soft vinyl chloride graft copolymer having excellent transparency is obtained by blending 0.5 to 50 parts by weight of a phenol resin with 100 parts by weight of a soft vinyl chloride graft copolymer obtained by polymerizing I was able to get it.

従来、軟質塩化ビニル系グラフト共重合体の透明性につ
いては、その重要性にもかかわらず、わずかにグラフト
重合法による改良が行われているのみで、ブレンドとい
う簡単な方法での改良は知られていない。
Conventionally, despite its importance, the transparency of soft vinyl chloride-based graft copolymers has only been slightly improved by graft polymerization, and improvements by the simple method of blending are unknown. Not yet.

本発明者らは軟質塩化ビニル系グラフト共重体の性能を
保持しつつ、透明性の改良を特定の割合のフェノール樹
脂をブレンドすることにより容易に行うことができるこ
とを見出し本発明に到達した。
The present inventors have discovered that while maintaining the performance of a soft vinyl chloride-based graft copolymer, the transparency can be easily improved by blending a phenol resin in a specific proportion, and have arrived at the present invention.

以下本発明を詳細に説明する。The present invention will be explained in detail below.

本発明(こおいて使用される軟質EVA一塩化ビニルグ
ラフト共重合体はEVAI 5〜70重量部の存在下に
、塩化ビニルモノマーもしくは塩化ビニルモノマーを主
体とするモノマー混合物30〜85重量部を重合させる
ことにより得られる。
The soft EVA monochloride graft copolymer used in the present invention is prepared by polymerizing 30 to 85 parts by weight of a vinyl chloride monomer or a monomer mixture mainly composed of vinyl chloride monomers in the presence of 5 to 70 parts by weight of EVAI. It can be obtained by

EVAに塩化ビニルモノマーをグラフト重合する方法と
して懸濁重合法が通常用いられるが、乳化重合、バルク
重合、溶液重合のいずれの方法で製造されたものでもよ
い。
Suspension polymerization is usually used as a method for graft polymerizing vinyl chloride monomers to EVA, but any method such as emulsion polymerization, bulk polymerization, or solution polymerization may be used.

EVAと塩化ビニルモノマーの重量比は7 0/3 0
〜15/85の範囲であり、7 0/3 0より大きく
なると軟質塩化ビニル樹脂特有のしなやかさに欠け、プ
ロツキング等により取扱いも難しくなり、15/85未
満では柔軟さが得られない。
The weight ratio of EVA and vinyl chloride monomer is 70/30
-15/85, and if it is greater than 70/30, it lacks the flexibility characteristic of soft vinyl chloride resins and becomes difficult to handle due to blocking, etc., and if it is less than 15/85, flexibility cannot be obtained.

EVAは高圧法、溶液法など従来知られているいずれの
プロセスで製造されたものでもよくエチレン戊分が35
〜75重量%のものが使用される。
EVA can be manufactured by any conventional process such as high pressure method or solution method.
~75% by weight is used.

エチレン戊分が35重量%未満のEVAは低温特性が悪
いため得られるグラフト共重合体は低温可撓性に欠け、
75重量%より多くなればEVAはかたくなり軟質塩化
ビニルグラフト共重合体を得るには適さない。
EVA with an ethylene fraction of less than 35% by weight has poor low-temperature properties, so the resulting graft copolymer lacks low-temperature flexibility.
If the amount exceeds 75% by weight, EVA becomes hard and is not suitable for obtaining a soft vinyl chloride graft copolymer.

また、EVAのメルトインデツクスは0.1〜4 0
0 g7’10Tni1tの範囲のものが使用される。
In addition, the melt index of EVA is 0.1 to 40.
A range of 0 g7'10Tnilt is used.

なお、塩化ビニルモノマーと混合して共重合するモノマ
ーとしては、エチルアクリレート、メチルアクリレート
、オクチルアクリレート、メチルメタクリレートなどの
アクリル酸誘導体やメタクリル酸誘導体、エチレン、プ
ロピレンなどのオレフイン、フマル酸およびマレイン酸
エステル、ビニルエーテルオヨび酢酸ビニル、プロピオ
ン酸ビニルなどのビニルエステルなどがあげられる。
Monomers that can be copolymerized by mixing with vinyl chloride monomers include acrylic acid derivatives and methacrylic acid derivatives such as ethyl acrylate, methyl acrylate, octyl acrylate, and methyl methacrylate, olefins such as ethylene and propylene, fumaric acid, and maleic acid esters. Examples include vinyl esters such as vinyl ether, vinyl acetate, and vinyl propionate.

本発明において用いられるフェノール樹脂としてはフェ
ノール、レゾルシノール、クレゾール、キシレノール、
p−t−プチルフェノール、pフエニルフェノールなど
のフェノール類とホルムアルデヒドとの縮合あるいは共
縮合反応により生戒されるフェノールホルムアルデヒド
樹脂で比重0.95〜1.30、環球式軟化点25〜1
80℃の性質を有しているものである。
Phenol resins used in the present invention include phenol, resorcinol, cresol, xylenol,
A phenol-formaldehyde resin produced by the condensation or co-condensation reaction of phenols such as pt-butylphenol and p-phenylphenol with formaldehyde, with a specific gravity of 0.95 to 1.30 and a ring and ball softening point of 25 to 1.
It has a property of 80°C.

一般にメチロール基含有量の極く少ない非熱反応型のも
のと、多くのメチロール基を有する熱反応型のものとが
あり、両方共、透明性の改良にその効果を発揮するが、
特に非熱反応型のものは溶融流動性を改良する効果があ
り、加工性の点からもすぐれている。
In general, there are non-thermally reactive types with extremely low methylol group content and thermally reactive types with many methylol groups, and both are effective in improving transparency.
In particular, non-thermal reaction type ones have the effect of improving melt fluidity and are also excellent in terms of processability.

軟質塩化ビニル系グラフト共重合体の透明性の改良にお
いて、十分な効果を発揮するためには軟質塩化ビニル系
グラフト共重合体100重量部に対して、フェノール樹
脂0.5〜50重量部であることが必要である。
In order to exhibit a sufficient effect in improving the transparency of the soft vinyl chloride graft copolymer, the amount of phenol resin should be 0.5 to 50 parts by weight per 100 parts by weight of the soft vinyl chloride graft copolymer. It is necessary.

0.5重量部未満では透明性の改良の効果が小さく、5
0重量部より多くなると柔軟性が低下する。
If it is less than 0.5 parts by weight, the effect of improving transparency is small;
When the amount exceeds 0 parts by weight, flexibility decreases.

軟質塩化ビニル系グラフト共重合体とフェノール樹脂は
混合および、あるいは混練させて均一な樹脂組成物とす
る。
The soft vinyl chloride graft copolymer and the phenol resin are mixed and/or kneaded to form a uniform resin composition.

その混合および混線の方法としては一軸または二軸押出
機で溶融混練する方法、ロール、バンバリーミキサー等
で混練する方法がとられる。
The mixing and cross-mixing methods include melt-kneading using a single-screw or twin-screw extruder, kneading using rolls, a Banbury mixer, and the like.

混練温度は樹脂が溶融し分解を起さない範囲であればよ
いが通常100℃以上200℃以下で行われる。
The kneading temperature may be within a range where the resin melts and does not cause decomposition, but the kneading is usually carried out at 100°C or higher and 200°C or lower.

混線時間は均一に混合された樹脂組成物となるまでの時
間を選択すればよい。
The mixing time may be determined by selecting the time required to obtain a uniformly mixed resin composition.

本発明Oこよる樹脂は従来の軟質塩化ビニル系グラフト
共重合体と同様、カレンダー加工、押出加工、射出或形
などの方法によりフイルム、シートパイプ、ホースなど
に加工される。
The resin according to the present invention can be processed into films, sheet pipes, hoses, etc. by methods such as calendering, extrusion, injection molding, etc. in the same manner as conventional soft vinyl chloride graft copolymers.

本発明によれば従来、その改良が困難であった透明性を
、他の性質をほとんど低下させることなく、安価な方法
での改良が可能である。
According to the present invention, transparency, which has conventionally been difficult to improve, can be improved at low cost without substantially reducing other properties.

本発明による軟質塩化ビニル系グラフト共重合体は、透
明性と可塑剤非移行性が要求される分野に特に有用であ
り、産業界への寄与は大きいものである。
The soft vinyl chloride-based graft copolymer according to the present invention is particularly useful in fields where transparency and plasticizer non-migration are required, and has made a significant contribution to industry.

以下に、実施例により本発明を具体的に説明するが本発
明をなんら制限するものではない。
EXAMPLES The present invention will be specifically explained below with reference to Examples, but the present invention is not limited in any way.

実施例1〜5比較例1 3インチロールを用いて、130℃にて、1o分間フェ
ノール樹脂の量を変えて、軟質塩化ビニルグラフト共重
合体と混練した。
Examples 1 to 5 Comparative Example 1 Using a 3-inch roll, varying amounts of phenol resin were kneaded with a soft vinyl chloride graft copolymer at 130° C. for 1 minute.

軟質塩化ビニルグラフト共重合体としては、酢酸ビニル
含有量40重量%、メルトインデックス75 g710
分のエチレンー酢酸ビニル共重合体60重量部の存在下
、塩化ビニルモノマー40重量部を懸濁重合法によりグ
ラフト重合することにより得られた樹脂を用いた。
The soft vinyl chloride graft copolymer has a vinyl acetate content of 40% by weight and a melt index of 75 g710.
A resin obtained by graft polymerizing 40 parts by weight of vinyl chloride monomer by suspension polymerization in the presence of 60 parts by weight of ethylene-vinyl acetate copolymer was used.

フェノール樹脂としては昭和ユニオン合成製CKM−2
400(環球式軟化点145℃、比重1.08の油溶性
非熱反応性フェノール樹脂)を用いた。
The phenol resin is CKM-2 manufactured by Showa Union Gosei.
400 (an oil-soluble nonthermally reactive phenolic resin with a ring and ball softening point of 145° C. and a specific gravity of 1.08) was used.

軟質塩化ビニル系グラフト共重合体安定剤として樹脂1
00重量部に対しジブチル錫ラウレート系安定剤1重量
部およびジブチル錫マレエート系安定剤1重量部を用い
た。
Resin 1 as a soft vinyl chloride graft copolymer stabilizer
1 part by weight of a dibutyltin laurate stabilizer and 1 part by weight of a dibutyltin maleate stabilizer were used per 00 parts by weight.

この樹脂組戒物を1朋厚のシートとし光線透過※※率と
ヘーズを測定した。
This resin composition was made into a 1-mm thick sheet and the light transmission rate and haze were measured.

結果を第1表に示す。第1表から特定の割合のフェノー
ル樹脂を配合した軟質塩化ビニル系グラフト共重合体は
曇りの少ない透明性にすぐれた樹脂であることがわかる
The results are shown in Table 1. From Table 1, it can be seen that the soft vinyl chloride graft copolymer blended with a specific proportion of phenol resin is a resin with excellent transparency and little haze.

また、軟質塩化ビニル系グラフト共重合体100重量部
にフェノール樹脂100重量部を配合した樹脂組或物は
柔軟性が低下したものとなった。
Furthermore, a resin composition in which 100 parts by weight of a phenolic resin was blended with 100 parts by weight of a soft vinyl chloride-based graft copolymer had decreased flexibility.

実施例6〜8比較例2 軟質塩化ビニル系グラフト共重合体として酢酸**ビニ
ル含有量32重量誇、メルトインデツクス3 0 .9
/1 0分のエチレンー酢酸ビニル共重合体45重量部
の存在下塩化ビニル七ノマー55重量部を懸濁重合法に
よりグラフト重合することにより得られた樹脂を用いて
実施例1〜5と同様の方法で混練し得られた樹脂組成物
の光線透過率とヘーズを測定した。
Examples 6 to 8 Comparative Example 2 As a soft vinyl chloride graft copolymer, the vinyl acetate content was over 32% by weight, and the melt index was 30. 9
The same procedure as in Examples 1 to 5 was carried out using a resin obtained by graft polymerizing 55 parts by weight of vinyl chloride heptanomer by a suspension polymerization method in the presence of 45 parts by weight of ethylene-vinyl acetate copolymer for 10 minutes. The light transmittance and haze of the resin composition obtained by kneading by the method were measured.

結果を第2表に示す。実施例 9 軟質塩化ビニル系グラフト共重合体として、酢酸ビニル
含有量40重量%、タルトインデックス7 5 ,9/
1 0分のエチレンー酢酸ビニル共重合体50重量部の
存在下塩化ビニルモノマー50重量部を懸濁重合法によ
りグラフト重合することにより得られた樹脂を用い、フ
ェノール樹脂として昭和ユニオン合戒製CKM2 10
3 (i球式軟化点110゜C1比重1.07の油溶性
非熱反応型フェノール樹脂を用い実施例1〜5と同様の
方法で混練し、得られた樹脂組成物の光線透過率とヘー
ズを測定した。
The results are shown in Table 2. Example 9 A soft vinyl chloride graft copolymer with a vinyl acetate content of 40% by weight and a tart index of 75,9/
Using a resin obtained by graft polymerizing 50 parts by weight of vinyl chloride monomer by suspension polymerization in the presence of 50 parts by weight of ethylene-vinyl acetate copolymer for 10 minutes, CKM2 10 manufactured by Showa Union Gokai was used as a phenol resin.
3 (i) An oil-soluble non-thermally reactive phenolic resin with a sphere softening point of 110° C1 and a specific gravity of 1.07 was kneaded in the same manner as in Examples 1 to 5, and the light transmittance and haze of the resulting resin composition were determined. was measured.

結果を第3表に示す。The results are shown in Table 3.

Claims (1)

【特許請求の範囲】[Claims] 1 エチレン戒分が35〜75重量%であるエチレンー
酢酸ビニル共重合体15〜70重量部の存在下{こ塩化
ビニル七ノマーもしくは塩化ビニル七ノマーを主体とす
るモノマー混合物30〜85重量部を重合させることに
より得られる軟質塩化ビニル系グラフト共重合体100
重量部とフェノール樹脂0.5〜50重量部からなる透
明性にすぐれた樹脂組或物。
1 In the presence of 15 to 70 parts by weight of an ethylene-vinyl acetate copolymer having an ethylene content of 35 to 75% by weight {polymerization of 30 to 85 parts by weight of vinyl chloride heptanomer or a monomer mixture mainly composed of vinyl chloride heptanomer Soft vinyl chloride graft copolymer 100 obtained by
A resin assembly with excellent transparency consisting of 0.5 to 50 parts by weight of phenolic resin and 0.5 to 50 parts by weight of phenolic resin.
JP14301580A 1980-10-15 1980-10-15 resin composition Expired JPS5836015B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14301580A JPS5836015B2 (en) 1980-10-15 1980-10-15 resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14301580A JPS5836015B2 (en) 1980-10-15 1980-10-15 resin composition

Publications (2)

Publication Number Publication Date
JPS5767646A JPS5767646A (en) 1982-04-24
JPS5836015B2 true JPS5836015B2 (en) 1983-08-06

Family

ID=15328950

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14301580A Expired JPS5836015B2 (en) 1980-10-15 1980-10-15 resin composition

Country Status (1)

Country Link
JP (1) JPS5836015B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6161113U (en) * 1984-06-18 1986-04-24
JPH02212007A (en) * 1989-02-13 1990-08-23 Suzuki Motor Co Ltd hole processing machine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6161113U (en) * 1984-06-18 1986-04-24
JPH02212007A (en) * 1989-02-13 1990-08-23 Suzuki Motor Co Ltd hole processing machine

Also Published As

Publication number Publication date
JPS5767646A (en) 1982-04-24

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