JPH0428026B2 - - Google Patents

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Publication number
JPH0428026B2
JPH0428026B2 JP26579985A JP26579985A JPH0428026B2 JP H0428026 B2 JPH0428026 B2 JP H0428026B2 JP 26579985 A JP26579985 A JP 26579985A JP 26579985 A JP26579985 A JP 26579985A JP H0428026 B2 JPH0428026 B2 JP H0428026B2
Authority
JP
Japan
Prior art keywords
weight
parts
vinyl
polyvinyl chloride
tetrahydrofuran
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
JP26579985A
Other languages
Japanese (ja)
Other versions
JPS62127337A (en
Inventor
Norio Takahata
Yoshihisa Kato
Manabu Yamazaki
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.)
Hitachi Cable Ltd
Original Assignee
Hitachi Cable 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 Hitachi Cable Ltd filed Critical Hitachi Cable Ltd
Priority to JP26579985A priority Critical patent/JPS62127337A/en
Publication of JPS62127337A publication Critical patent/JPS62127337A/en
Publication of JPH0428026B2 publication Critical patent/JPH0428026B2/ja
Granted legal-status Critical Current

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Description

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

[産業上の利用分野] 本発明は、表面艶消しおよび非移行性の成形品
を得るためのビニル樹脂組成物に関するものであ
る。 [従来の技術] ポリ塩化ビニル樹脂組成物では、可撓性、耐寒
性、加工性等を付与するために可塑性が使用され
るのが一般的である。ポリ塩化ビニル樹脂におい
てはこの可塑剤の応用がその用途拡大に著しく関
係しており、この発展は可塑剤によるところが大
であると云われているゆえんである。 しかしながら、可塑剤は分子量500以下の液状
体であり、他の物質への移行や揮散を生じ、これ
が用途によつて大きな欠点となつている。 このような欠点を補うため、可塑剤に代えてポ
リ塩化ビニル樹脂と相溶性のあるポリマ、例え
ば、エチレン−酢酸ビニル共重合体、ポリウエタ
ン、アクリロニトリルブタジエン等を使用するこ
とが知られている。これらのポリマは、分子量も
大きいため移行、揮散の欠点が解消され、非移行
性や非揮散性の用途において重宝されている。 一方、最近、列車、自動車、室内、電線・ケー
ブルなどの幅広い分野においてポリ塩化ビニル樹
脂組成物がもつ本来の表面光沢が、ビニル的光沢
あるいは安物光沢などといわれて嫌われ、艶消し
状肌表面の製品の要求が増加している。可塑剤を
用いたものあるいは相溶性のポリマを用いたもの
のいずれにもポリ塩化ビニル樹脂特有の光沢が発
現する。 この解決策として、炭酸カルシウム、無水ケイ
酸等の無機充填剤を添加する方法、ポリ塩化ビニ
ル樹脂の分子量、すなわち重合度を増加する方法
など、多くの艶消し法が提案されてきている。 [発明が解決しようとする問題点] しかしながら、これらのいずれの方法において
も、特性上に問題が生じたり、艶消し効果が不均
一であつたり、成形加工性が悪化するという問題
があり、所望する艶消し状態で安定した製品を得
ることは困難であつた。 本発明は上記に基いてなされたものであつて、
表面光沢のない艶消し状表面を有し、しかも非移
行性の成形品を得ることができるビニル樹脂組成
物の提供を目的とするものである。 [問題点を解決するための手段] 本発明の樹脂組成物は、エチレン−酢酸ビニル
共重合体またはポリウレタンを骨格とし、これに
塩化ビニルをグラフト共重合したグラフト共重合
の少なくとも1種と、テトラヒドロフラン不溶ゲ
ル分が5〜90重量%で残部がテトラヒドロフラン
可溶分からなる部分架橋ポリ塩化ビニル樹脂とか
らなることを特徴とするものである。 テトラヒドロフラン不溶ゲル分をもつ部分架橋
ポリ塩化ビニル樹脂は、塩化ビニルの重合系にジ
アリルフタレート、ジアリルマレート、トリアリ
ルシアヌレート、トリアリルトリメリテート、ト
リメチロールプロパントリメタクリレート、ジビ
ニルベンゼン等の多官能性モノマを添加し、任意
量のゲル分を生成せしめるように重合する方法に
よつて製造されるものである。 本発明において、テトラヒドロフラン不溶ゲル
分とは、ソツクスレー抽出器で熱テトラヒドロフ
ランにより20時間抽出後、350メツシユで分離さ
れる抽出残渣のことをいう。本発明においては、
この値は5〜90重量%のものを使用する必要があ
り、5重量%未満のものでは艶消し効果が得られ
ず、90重量%を越えると加工性に問題が生ずるこ
とになる。 なお、この加工性には当然残部のテトラヒドロ
フラン可溶部の重合度等も関係するが、これら残
部の重合度は特に加工性に問題なければ限定しな
いが一般的には平均重合度は500〜3000が好まし
い。 本発明は、非移行性を主にねらつたものである
ため、液状可塑剤の使用は好ましくないが、非移
行性を実現できる範囲内での使用は可能であり、
ポリエステル、エポキシ化大豆油、トリメリツト
酸エステル、フタル酸エステル等を目的に応じて
使用できる。 その他、安定剤、滑剤、難燃剤、着色剤、改質
剤、酸化防止剤、充填剤、加工助剤、紫外線吸収
剤など、通常のビニル樹脂に使用される配合剤類
は当然のことながら使用可能である。 [実施例] 実施例 1 エチレン−酢酸ビニル−塩化ビニルグラフト共
重合体(酢酸ビニル量45重量%のエチレン−酢酸
ビニル共重合体含有量45重量部と塩化ビニル55重
量部を含有)100重量部、ゲル分5重量%の部分
架橋ポリ塩化ビニル樹脂50重量部、三塩基性硫酸
鉛10重量部、ステアリン酸鉛1重量部、フエノー
ル系酸化防止剤(イルガノツクス1010)0.5重量
部、三酸化アンチモン5重量部をロール混練後ペ
レツト化し、これを40m/m押出機にてシートを
押出した。 実施例 2 実施例1で用いたと同様のエチルン−酢酸ビニ
ル−塩化ビニルグラフト共重合体100重量部、ゲ
ル分90重量%の部分架橋ポリ塩化ビニル樹脂20重
量部、三塩基性硫酸鉛10重量部、ステアリン酸1
重量部、フエノール系酸化防止剤(イルガノツク
ス1010)0.5重量部、三酸化アンチモン5重量部
をロール混練後ペレツト化し、これを40m/m押
出機にてシートを押出した。 実施例 3 実施例1で用いたと同様のエチレン−酢酸ビニ
ル−塩化ビニルグラフト50重量部、ポリウレタン
−塩化ビニルグラフト共重合体(ポリウレタン50
重量部の塩化ビニル50重量部を含有)50重量部、
ゲル分20重量%の部分架橋ポリ塩化ビニル樹脂30
重量部、三塩基性硫酸鉛10重量部、ステアリン酸
1重量部、フエノール系酸化防止剤(イルガノツ
クス1010)0.5重量部、三酸化アンチモン5重量
部をロール混練後ペレツト化し、これを40m/m
押出機にてシートを押出した。 実施例 4 実施例1で用いたと同様のエチレン−酢酸ビニ
ル−塩化ビニルグラフト共重合体100重量部、ゲ
ル分20重量%の部分架橋ポリ塩化ビニル樹脂30重
量部、三塩基性硫酸鉛10重量部、ステアリン酸1
重量部、フエノール系酸化防止剤(イルガノツク
ス1010)0.5重量部、三酸化アンチモン5重量部、
多官能モノマ(トリメチロールプロパントリマタ
クリレート)10重量部をロール混練後ペレツト化
し、これを40m/m押出機にてシートを押出し
た。続いてこのシートに電子線を5Mrad照射し
て架橋した。 実施例 5 ポリウレタン−塩化ビニルグラフト共重合体
(ポリウレタン50重量部と塩化ビニル50重量部を
含有)100重量部、ゲル分5重量%の部分架橋ポ
リ塩化ビニル樹脂50重量部、三塩基性硫酸鉛10重
量部、ステアリン酸鉛1重量部、フエノール系酸
化防止剤(イルガノツクス1010)0.5重量部、三
酸化アンチモン5重量部をロール混練後ペレツト
化し、これを40m/m押出機にてシート押出し
た。 比較例 1 実施例1で用いたと同様のエチレン−酢酸ビニ
ル−塩化ビニルグラフト共重合体100重量部、ゲ
ル分3重量%の部分架橋ポリ塩化ビニル樹脂20重
量部、三塩基性硫酸鉛10重量部、ステアリン酸1
重量部、フエノール系酸化防止剤(イルガノツク
ス1010)0.5重量部、三酸化アンチモン5重量部
をロール混練後ペレツト化し、これを40m/m押
出機にてシートを押出した。 比較例 2 実施例1で用いたと同様のエチレン−酢酸ビニ
ル−塩化ビニルグラフト共重合体100重量部、ゲ
ル分95重量%の部分架橋ポリ塩化ビニル樹脂20重
量部、三塩基性硫酸鉛10重量部、ステアリン酸1
重量部、フエノール系酸化防止剤(イルガノツク
ス1010)0.5重量部、三酸化アンチモン5重量部
をロール混練後ペレツト化し、これを40m/m押
出機にてシートを押出した。 従来例 重合度1300のポリ塩化ビニル樹脂100重量部、
ジオクチルフタレート60重量部、三塩基性硫酸鉛
10重量部、ステアリン酸1重量部をロール混練後
ペレツト化し、これを40m/m押出機にてシート
を押出した。 以上の各実施例、各比較例および従来例により
作製したシート評価結果を第1表に示す。 なお、評価は次のようにして行つた。 加工性:160℃に設定した6インチロールで混練
したときの加工性(巻付き、混練性)およびヘ
ツド、ダイ部温度190℃の40m/m押出機
(L/D≒21、圧縮比3.0)におけるシート(厚
さ1mm、幅50mm)の押出加工性から判定した。 艶消し状態:40m/m押出機で押出したシート表
面の状態を肉眼で観察して判定した。 ゲル分率:初期重量(A)測定後、70℃テトラヒドロ
フラン中に24時間浸漬後取出し、80℃で4時間
乾燥後の重量(B)を測定し、(B/A)×100で求
めた。 非移行性:押出シートを厚さ1mmのポリエチレン
シートに重ねて50℃で24時間放置後ポリエチレ
ン表面の侵食、軟化、汚損の状態で判定。 揮発減量:100℃−168時間老化前後の重量より求
めた。
[Industrial Field of Application] The present invention relates to a vinyl resin composition for obtaining a molded article with a matte surface and non-migrating properties. [Prior Art] In polyvinyl chloride resin compositions, plasticity is generally used to impart flexibility, cold resistance, processability, and the like. The application of plasticizers in polyvinyl chloride resins is significantly related to the expansion of their uses, and this development is said to be largely due to the plasticizers. However, plasticizers are liquid substances with a molecular weight of 500 or less, and may migrate to other substances or volatilize, which is a major drawback depending on the application. In order to compensate for these drawbacks, it is known to use a polymer compatible with polyvinyl chloride resin, such as ethylene-vinyl acetate copolymer, polyurethane, acrylonitrile butadiene, etc., in place of the plasticizer. These polymers have large molecular weights, so they overcome the drawbacks of migration and volatilization, and are useful in non-migration and non-volatility applications. On the other hand, in recent years, the inherent surface gloss of polyvinyl chloride resin compositions has been disliked in a wide range of fields such as trains, automobiles, interior rooms, and electric wires and cables, and has been disliked as having a vinyl-like luster or cheap luster, resulting in a matte skin surface. The demand for products is increasing. Both those using plasticizers and those using compatible polymers exhibit the gloss peculiar to polyvinyl chloride resin. As a solution to this problem, many matting methods have been proposed, including methods of adding inorganic fillers such as calcium carbonate and silicic anhydride, and methods of increasing the molecular weight of polyvinyl chloride resin, that is, the degree of polymerization. [Problems to be Solved by the Invention] However, in any of these methods, there are problems in terms of properties, non-uniform matting effect, and deterioration in moldability. It was difficult to obtain a stable product in a matte state. The present invention has been made based on the above, and includes:
The object of the present invention is to provide a vinyl resin composition that has a matte surface with no surface gloss and is capable of producing non-migration molded products. [Means for Solving the Problems] The resin composition of the present invention comprises at least one type of graft copolymer in which vinyl chloride is grafted onto an ethylene-vinyl acetate copolymer or a polyurethane skeleton, and tetrahydrofuran. It is characterized in that it consists of a partially crosslinked polyvinyl chloride resin having an insoluble gel content of 5 to 90% by weight and the remainder being a tetrahydrofuran soluble content. Partially crosslinked polyvinyl chloride resin with tetrahydrofuran-insoluble gel content contains polyfunctional compounds such as diallyl phthalate, diallyl maleate, triallyl cyanurate, triallyl trimellitate, trimethylolpropane trimethacrylate, and divinylbenzene in the vinyl chloride polymerization system. It is manufactured by a method in which a polymeric monomer is added and polymerized to produce an arbitrary amount of gel content. In the present invention, the term "tetrahydrofuran-insoluble gel" refers to the extraction residue separated using 350 meshes after 20 hours of extraction with hot tetrahydrofuran in a Soxhlet extractor. In the present invention,
It is necessary to use a material with this value of 5 to 90% by weight; if it is less than 5% by weight, a matte effect cannot be obtained, and if it exceeds 90% by weight, problems will arise in processability. Note that this processability is naturally related to the degree of polymerization of the remaining tetrahydrofuran soluble portion, but the degree of polymerization of these remaining portions is not limited unless there is a problem with processability, but generally the average degree of polymerization is 500 to 3000. is preferred. Since the present invention mainly aims at non-migrating properties, it is not preferable to use liquid plasticizers, but it is possible to use them within the range where non-migrating properties can be achieved.
Polyester, epoxidized soybean oil, trimellitic acid ester, phthalic acid ester, etc. can be used depending on the purpose. In addition, compounding agents used in ordinary vinyl resins, such as stabilizers, lubricants, flame retardants, colorants, modifiers, antioxidants, fillers, processing aids, and ultraviolet absorbers, are of course used. It is possible. [Examples] Example 1 100 parts by weight of ethylene-vinyl acetate-vinyl chloride graft copolymer (containing 45 parts by weight of ethylene-vinyl acetate copolymer containing 45 parts by weight of vinyl acetate and 55 parts by weight of vinyl chloride) , 50 parts by weight of partially cross-linked polyvinyl chloride resin with a gel content of 5% by weight, 10 parts by weight of tribasic lead sulfate, 1 part by weight of lead stearate, 0.5 parts by weight of phenolic antioxidant (Irganox 1010), 5 parts by weight of antimony trioxide. Parts by weight were kneaded with rolls and turned into pellets, which were then extruded into a sheet using a 40 m/m extruder. Example 2 100 parts by weight of the same ethylne-vinyl acetate-vinyl chloride graft copolymer used in Example 1, 20 parts by weight of a partially crosslinked polyvinyl chloride resin with a gel content of 90% by weight, and 10 parts by weight of tribasic lead sulfate. , stearic acid 1
Parts by weight, 0.5 parts by weight of a phenolic antioxidant (Irganox 1010), and 5 parts by weight of antimony trioxide were kneaded with rolls and formed into pellets, which were extruded into a sheet using a 40 m/m extruder. Example 3 50 parts by weight of ethylene-vinyl acetate-vinyl chloride graft similar to that used in Example 1, polyurethane-vinyl chloride graft copolymer (polyurethane 50 parts by weight)
(containing 50 parts by weight of vinyl chloride) 50 parts by weight,
Partially cross-linked polyvinyl chloride resin 30 with gel content of 20% by weight
Parts by weight, 10 parts by weight of tribasic lead sulfate, 1 part by weight of stearic acid, 0.5 parts by weight of a phenolic antioxidant (Irganox 1010), and 5 parts by weight of antimony trioxide were kneaded with rolls and pelletized.
The sheet was extruded using an extruder. Example 4 100 parts by weight of the same ethylene-vinyl acetate-vinyl chloride graft copolymer used in Example 1, 30 parts by weight of partially crosslinked polyvinyl chloride resin with a gel content of 20% by weight, and 10 parts by weight of tribasic lead sulfate. , stearic acid 1
parts by weight, 0.5 parts by weight of phenolic antioxidant (Irganox 1010), 5 parts by weight of antimony trioxide,
10 parts by weight of a polyfunctional monomer (trimethylolpropane trimacrylate) was roll-kneaded and pelletized, which was then extruded into a sheet using a 40 m/m extruder. Subsequently, this sheet was crosslinked by irradiating it with an electron beam of 5 Mrad. Example 5 100 parts by weight of polyurethane-vinyl chloride graft copolymer (containing 50 parts by weight of polyurethane and 50 parts by weight of vinyl chloride), 50 parts by weight of partially crosslinked polyvinyl chloride resin with a gel content of 5% by weight, tribasic lead sulfate 10 parts by weight of lead stearate, 0.5 parts by weight of a phenolic antioxidant (Irganox 1010), and 5 parts by weight of antimony trioxide were roll-kneaded and formed into pellets, which were extruded into sheets using a 40 m/m extruder. Comparative Example 1 100 parts by weight of the same ethylene-vinyl acetate-vinyl chloride graft copolymer used in Example 1, 20 parts by weight of partially crosslinked polyvinyl chloride resin with a gel content of 3% by weight, and 10 parts by weight of tribasic lead sulfate. , stearic acid 1
Parts by weight, 0.5 parts by weight of a phenolic antioxidant (Irganox 1010), and 5 parts by weight of antimony trioxide were kneaded with rolls and formed into pellets, which were extruded into a sheet using a 40 m/m extruder. Comparative Example 2 100 parts by weight of the same ethylene-vinyl acetate-vinyl chloride graft copolymer used in Example 1, 20 parts by weight of partially crosslinked polyvinyl chloride resin with a gel content of 95% by weight, and 10 parts by weight of tribasic lead sulfate. , stearic acid 1
Parts by weight, 0.5 parts by weight of a phenolic antioxidant (Irganox 1010), and 5 parts by weight of antimony trioxide were kneaded with rolls and formed into pellets, which were extruded into a sheet using a 40 m/m extruder. Conventional example: 100 parts by weight of polyvinyl chloride resin with a degree of polymerization of 1300,
60 parts by weight of dioctyl phthalate, tribasic lead sulfate
10 parts by weight of stearic acid and 1 part by weight of stearic acid were kneaded with rolls and formed into pellets, which were then extruded into a sheet using a 40 m/m extruder. Table 1 shows the evaluation results of sheets produced according to the above examples, comparative examples, and conventional examples. The evaluation was conducted as follows. Processability: Processability (wrapping, kneading properties) when kneading with a 6-inch roll set at 160℃ and a 40m/m extruder with a head and die temperature of 190℃ (L/D≒21, compression ratio 3.0) Judgment was made from the extrusion processability of a sheet (thickness: 1 mm, width: 50 mm). Matte state: Determined by visually observing the state of the sheet surface extruded with a 40 m/m extruder. Gel fraction: After measuring the initial weight (A), it was immersed in tetrahydrofuran at 70°C for 24 hours and then taken out, and the weight (B) after drying at 80°C for 4 hours was measured and calculated by (B/A) x 100. Non-migration: The extruded sheet is stacked on a 1 mm thick polyethylene sheet and left at 50℃ for 24 hours, and then judged by the state of erosion, softening, and staining on the polyethylene surface. Volatilization loss: Calculated from the weight before and after aging at 100°C for 168 hours.

【表】 第1表からも明らかな通り、本発明の範囲にあ
る実施例1〜4では各特性においてバランスのと
れたものとなつている。 これに対し、比較例1はテトラヒドロフラン不
溶分の含有量が規定値以下のもので、艶が生じ
た。比較例2はテトラヒドロフラン不溶分の含有
量が規定値以上のもので、加工性が悪く、試料の
作成ができなかつた。 [発明の効果] 以上の説明から明らかな通り、本発明によれ
ば、非移行性、非揮散性であり、しかも表面の艶
を消したビニル成形品を得ることができるように
なる。
[Table] As is clear from Table 1, Examples 1 to 4 within the scope of the present invention are well-balanced in each characteristic. On the other hand, in Comparative Example 1, the content of tetrahydrofuran insoluble matter was less than the specified value, and gloss appeared. In Comparative Example 2, the content of tetrahydrofuran-insoluble matter exceeded the specified value, and the processability was poor, making it impossible to prepare a sample. [Effects of the Invention] As is clear from the above description, according to the present invention, it is possible to obtain a vinyl molded product that is non-migratable, non-volatile, and has a matte surface.

Claims (1)

【特許請求の範囲】[Claims] 1 エチレン−酢酸ビニル共重合体またはポリウ
レタンを骨格とし、これに塩化ビニルをグラフト
共重合体したグラフト共重合体の少なくとも1種
と、テトラヒドロフラン不溶ゲル分が5〜90重量
%で残部がテトラヒドロフラン可溶分からなる部
分架橋ポリ塩化ビニル樹脂とからなることを特徴
とするビニル樹脂組成物。
1 At least one type of graft copolymer having an ethylene-vinyl acetate copolymer or a polyurethane skeleton and graft copolymerizing vinyl chloride thereon, and a tetrahydrofuran-insoluble gel content of 5 to 90% by weight, and the remainder being tetrahydrofuran-soluble. A vinyl resin composition comprising a partially crosslinked polyvinyl chloride resin consisting of:
JP26579985A 1985-11-26 1985-11-26 vinyl resin composition Granted JPS62127337A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26579985A JPS62127337A (en) 1985-11-26 1985-11-26 vinyl resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26579985A JPS62127337A (en) 1985-11-26 1985-11-26 vinyl resin composition

Publications (2)

Publication Number Publication Date
JPS62127337A JPS62127337A (en) 1987-06-09
JPH0428026B2 true JPH0428026B2 (en) 1992-05-13

Family

ID=17422198

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26579985A Granted JPS62127337A (en) 1985-11-26 1985-11-26 vinyl resin composition

Country Status (1)

Country Link
JP (1) JPS62127337A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0368644A (en) * 1989-08-09 1991-03-25 Sumitomo Bakelite Co Ltd Vinyl chloride resin composition
JP5741562B2 (en) * 2012-12-04 2015-07-01 ダイキン工業株式会社 Dust collector

Also Published As

Publication number Publication date
JPS62127337A (en) 1987-06-09

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