JPH0157138B2 - - Google Patents

Info

Publication number
JPH0157138B2
JPH0157138B2 JP17274785A JP17274785A JPH0157138B2 JP H0157138 B2 JPH0157138 B2 JP H0157138B2 JP 17274785 A JP17274785 A JP 17274785A JP 17274785 A JP17274785 A JP 17274785A JP H0157138 B2 JPH0157138 B2 JP H0157138B2
Authority
JP
Japan
Prior art keywords
vinyl chloride
copolymer
bisphenol
polymerization
vinyl
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
JP17274785A
Other languages
Japanese (ja)
Other versions
JPS6143645A (en
Inventor
Kazumasa Yamane
Masahiro Kobayashi
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry 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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP17274785A priority Critical patent/JPS6143645A/en
Publication of JPS6143645A publication Critical patent/JPS6143645A/en
Publication of JPH0157138B2 publication Critical patent/JPH0157138B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

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、艶消にすぐれ、かつ表面凹凸が均一
な成形品を与える塩化ビニル系共重合体のうち、
特に著しく熱安定性の改良された塩化ビニル系共
重合体を含む塩化ビニル系樹脂組成物に関する。
更に詳しくは、塩化ビニル、又は更に塩化ビニル
共重合可能な単量体一種以上の混合物と後記一般
式(1)で示されるビスフエノールA変性ジアクリレ
ート又は、ビスフエノールA変性ジメタクリレー
トを共重合して得られる塩化ビニル系共重合体を
含む樹脂組成物に関するものであり、それから得
られる成形品は艶消が容易で、かつ成形品の表面
凹凸が非常に均一となり、熱安定性が著しく良好
である。 塩化ビニル系樹脂は安価であり、その成形品は
機械的特性、耐候性、耐油性等にすぐれる事から
種々の分野に於いて巾広く使用されている。 (従来の技術と問題点) しかし乍ら、塩化ビニル系樹脂は通常の加工条
件では、成形品の表面を艶消にする事は出来ず、
また艶消にする為に加工温度を低くしたりあるい
は充填剤を多量に使用すると機械的特性が低下す
る等の欠点があり、さらに又エンボス加工、アク
リル塗装によつて艶消にすると成形品のコストが
高くなる等の不都合があつた。 しかるに近年、種々の分野の成形品に於いて、
高級感のある艶消表面が好まれる様になり、しか
も機械的強度、触感の良さという観点から表面凹
凸が均一で、きめ細かな表面状態が好まれる様に
なつてきた。 これ等の要望にこたえるべく、すでにジアリル
フタレート、ジアリルマレエート、ポリエチレン
グリコールジアクリレート、ポリエチレングリコ
ールジメタクリレート等の架橋剤を使用して重合
中にゲル分を生成せしめ艶消表面を得るという提
案(特開昭54−80354、特開昭56−5843等)があ
るが、これ等の技術によつて得られる塩化ビニル
系重合体は、いずれも通常の塩化ビニル樹脂に比
較して熱安定性が著しく劣り、通常の塩化ビニル
樹脂の加工件に於いては、熱安定剤を多量に使用
する必要がありコストが高くなる、又、加工条件
の変更、例えば加工温度を下げる等の操作によつ
て熱安定性の悪さをカバーしようとすると十分に
混練する事が出来ず、成形品の物性が低下する等
の欠点があつた。 (問題点を解決するための手段) これ等の欠点を改良すべく、鋭意研究を進めた
結果、後記一般式(1)で示されるビスフエノールA
変性ジアクリレート又は、ビスフエノールA変性
ジメタクリレートを使用すると熱安定性が著しく
改良されるという事を見い出し、本発明を完成す
るに到つた。 即ち本発明は、塩化ビニル、又は更に塩化ビニ
ルと共重合可能な単量体1種以上の混合物と下記
一般式(1)で示されるビスフエノールA変性ジアク
リレート又はビスフエノールA変性ジメタクリレ
ートを共重合してなる塩化ビニル系共重合体と、
通常の塩化ビニル樹脂又は、塩化ビニル系樹脂と
からなる塩化ビニル系樹脂組成物を内容とする。 (Xは水素原子、メチル基、水酸基から選ばれる
基、nは1〜80の整数) 本発明の主たる目的は、塩化ビニル、又は更に
塩化ビニルと共重合可能な単量体1種以上の混合
物と前記一般式(1)で示されるビスフエノールA変
性ジアクリレート又はビスフエノールA変性ジメ
タクリレートを共重合して得られる塩化ビニル系
共重合体を使用する事によつて表面凹凸が均一
で、きめが細かく、従つて触感が良好で、かつ艶
消となる成形品を容易に得る事の出来る塩化ビニ
ル系共重合体を含む塩化ビニル系樹脂組成物を提
供する事にある。即ち、該共重合体を含む樹脂組
成物に安定剤、滑剤、抗酸化剤、ゴム類、紫外線
吸収剤、加工助剤、顔料等を配合して加工する事
によつて硬質分野に於ける各種の成形品を、又さ
らに可塑剤を加えて軟質化する事によつて軟質分
野に於ける各種の成形品を、表面凹凸が均一で、
きめが細かく、触感が良好で、かつ艶消にする事
が出来る。 前記一般式(1)で示されるビスフエノールA変性
ジアクリレート、又はビスフエノールA変性ジメ
タクリレートを使用して得られる共重合体の熱安
定性が著しく向上する理由はまだ明確にはなつて
いない。しかし乍ら、従来より、ビスフエノール
Aの各種誘導体が熱安定剤としてポリ塩化ビニル
等に添加されている事からビスフエノール残基に
熱安定性改良効果がある事が推定される。又、両
末端の官能基による架橋によりゲル分が生成し成
形品中にゲル分が残留し、表面凹凸は均一で、き
め細かく、触感は良好でかつ艶消となる。 本発明に使用するビスフエノールA変性ジアク
リレート又はビスフエノールA変性ジメタクリレ
ートとしては、ビスコート#540、ビスコート
#700(以上大阪有機化学工業(株)製)、XD8008.01
(ダウ・ケミカル社製)等が市販されている。 本発明に成る塩化ビニル系共重合体は、懸濁重
合法、乳化重合法、塊状重合法、溶液重合法等、
従来知られている重合法であればいずれの重合方
法を用いても良いが、製造の容易さ、製造コスト
の観点から懸濁重合法による方法が好ましい。 本発明に於いて使用する該化合物の量は、塩化
ビニル単量体100重量部に対し、0.001重量部〜15
重量部が良く、特に好ましくは、0.01〜5重量部
が良い。又、該化合物を添加するに際しては重合
途中に後添加する事の操作は、本発明の目的を損
なうものではない。 懸濁重合に於ける重合温度は特に限定しない
が、20℃から80℃が好ましい。又、重合途中に於
ける重合温度の変更等は本発明の目的を損なうも
のではない。懸濁重合において使用する開始剤
は、通常塩化ビニル樹脂の重合に使用されている
ものであればどの様なものでも良く、例えばラウ
リルパーオキサイド、ジ−2−エチルヘキシルパ
ーオキシジカーボネート、イソプロピルパーオキ
シジカーボネート、イソブチリルパーオキサイ
ド、3,5,5−トリメチルヘキサノイルパーオ
キサイド、t−ブチルパーオキシピバレート等の
有機過酸化物、アゾビスイソブチロニトリル、ア
ゾビスバレロニトリル等のアゾ系ラジカル開始剤
のうち1種又は2種以上を使用出来る。さらに、
これ等の開始剤を途中で添加する等の操作によつ
て本発明の目的が変るものではない。又、懸濁重
合で使用する分散剤としては、部分鹸化ポリ酢酸
ビニル、メチルセルロース、ヒドロキシプロポキ
シメチルセルロース、エチルセルロース、ヒドロ
キシエチルセルロース、ポリビニルピロリドン、
無水マレイン酸とメチルビニルエーテルとの共重
合体、ゼラチン、カゼイン、でんぷん等の有機高
分子分散剤、タルク、硫酸カルシウム、リン酸カ
ルシウム等の無機分散剤等の公知の分散剤を単独
又併用して使用出来る。さらに又、これ等の分散
剤を重合途中に後添加する等の操作を行なつても
本発明の目的を損なうものではない。 本発明に於いて、主鎖を形成する単量体は塩化
ビニル単独又は、少なくとも50重量%の塩化ビニ
ルと、これと共重合可能なビニル系単量体との混
合物である。この塩化ビニルと共重合可能な単量
体としては、酢酸ビニル等のビニルエステル類、
メチルビニルエーテル等のビニルエーテル類、ア
クリル酸又はメタクリル酸及びそのエステル、マ
レイン酸又はフマル酸及びそのエステルあるいは
無水物、芳香族ビニル化合物、ビニリデンハライ
ド、あるいは、モノオレフイン等のビニル系単量
体が例示される。また本発明においては、これ等
の単量体を途中で追加する等の操作をする事は何
等支障なく、これ等の単量体の反応性比に応じ
て、又、最終的に出来上る分子設計に応じて行な
う事が出来る。 さらに本発明においては、通常、塩化ビニル樹
脂の改質の為に行なわれている各種添加剤、例え
ば抗酸化剤、紫外線吸収剤、熱安定剤、滑剤、ゴ
ム類等の添加、あるいは、重合と安定に行なう為
に緩衝剤の添加等は本発明の主旨を何等変えるも
のでなく目的に応じて適宜採用できる。 本発明組成物中の共重合体は、硬質分野又は軟
質分野、両分野に於いて使用出来る。即ち、該共
重合体にゴム類、安定剤、滑剤、酸化防止剤、紫
外線吸収剤、加工助剤、顔料等を配合し加工する
事によつて硬質分野の成形品を得る。又、通常の
塩化ビニル系樹脂又は塩化ビニル樹脂に該共重合
体を併用し共重合体を含む樹脂組成物とする事に
よつて該共重合体の持つ特性を充分に発揮させ得
る。 本発明に於いて使用出来るゴム類としては、
NBR、EPDM、SBR、シリコンゴム、天然ゴ
ム、ポリブタジエン、ネオプレンゴム、イソプレ
ンゴム、MBS、EVA、等が挙げられる。安定剤
としては、スズ系安定剤、鉛系安定剤、金属石鹸
類、Ca−Zn系安定剤、Ba系安定剤等を1種又は
2種以上を併用する。滑剤としては、ポリエチレ
ンワツクス系滑剤、ステアリン酸系滑剤、アルコ
ール系滑剤等のうち1種又は2種以上を併用す
る。 本発明に於いて用いる弾常の塩化ビニル系樹脂
とは、少なくとも50重量%の塩化ビニルを含む共
重合体であつて、例えば、酢酸ビニル等のビニル
エステル類との共重合体、メチルビニルエーテル
等のビニルエーテル類との共重合体、アクリル酸
又はメタクリル酸及びそのエステル類との共重合
体、マレイン酸又はフマル酸又はイタコン酸及び
そのエステル類あるいは無水物との共重合体、芳
香族ビニル化合物との共重合体、ビニリデンハラ
イドあるいはモノオレフイン等のビニル系単量体
との共重合体等のうち1種又は2種以上を表わ
す。 さらに、該共重合体に可塑剤を添加する事によ
り軟質分野の成形品を得る事も出来る。使用出来
る可塑剤量は特に限定されるものではなく、必要
に応じて使用量を調節すれば良い。又、使用され
る可塑剤も特に限定されるものではなく、通常使
用されているフタル酸系可塑剤、エポキシ系可塑
剤、リン酸エステル系可塑剤、ポリエステル系可
塑剤等のうち1種又は2種以上を併用する事が出
来る。 (発明の効果) 本発明の塩化ビニル系共重合体を含む塩化ビニ
ル系樹脂組成物は成形品にしたとき艶消が容易
で、かつ成形品の表面凹凸が非常に均一となり、
更に実施例に示す通り熱安定性に優れている効果
を奏するので本発明は工業的に優れた樹脂組成物
である。 (実施例) 次に実施例により本発明の実施態様を更に明ら
かにするが、これ等は本発明の範囲を限定するも
のではない。 参考例 1〜8 内容積300のステンレス製重合器にイオン交
換水200部、部分鹸化ポリ酢酸ビニル0.2部、ジイ
ソプロピルパーオキサイド0.06部、ジ−2−エチ
ルヘキシルパーオキシジカーボネート0.06部、塩
化ビニルモノマー100部及び表−1に示す仕込量
のビスコート#540又はビスコート#700を添加
し、重合温度35℃で15時間重合した。得られたス
ラリーを脱水し、熱風乾燥機で5℃で18時間乾燥
し、各測定に供した。 比較例 1〜6 参考例と同様にして、イオン交換水、部分鹸化
ポリ酢酸ビニル、ジイソプロピルパーオキサイ
ド、ジ−2−エチルヘキシルパーオキシジカーボ
ネート、塩化ビニルモノマー及び表−1に示す架
橋剤を所定量仕込み重合温度35℃で15時間重合し
た。参考例と同様な方法で乾燥し、各測定に供し
た。尚、各物性値は次の様にして測定した。 (1) 試験片の作成:配合 サンプル共重合体 100重量部 ジオクチルフタレート 100 〃 三塩基性硫酸鉛 3 〃 ステアリン酸鉛 1 〃 炭酸カルシウム 30 〃 によつてブレンドを行ない、混合物をロール温
度185℃で10分間混練りし、厚さ約0.7m/mの
素練りシートを作製し、更にプレス温度190℃、
圧力200Kg/cm2の条件でプレス成形を行ない測
定用サンプルシートを作製した。 (2) 圧縮永久歪:JIS−K6301に準拠し、圧縮の
条件は圧縮率25%、温度70℃ 22時間とした。 (3) 抗張力:JIS−K6723に準拠しプレス成形シ
ートから試験片を打ち抜き、引張り試験機を用
い測定温度25℃、引張り速度200mm/分で測定
した。 (4) 脱HC1速度:オートマチツク滴定装置AT−
107(京都電子工業(株)製)を用いてオイルバス温
度235℃、N2流量20ml/分、滴定速度0.02ml/
秒、試料(素練りシートを約3mm2に切つたも
の)10gで、オイルバスに設置後、規定の
NaOH溶液使用量が5.0mlになるまでの時間を
求めた。
(Industrial Application Field) The present invention is directed to a vinyl chloride copolymer that provides molded products with excellent matteness and uniform surface irregularities.
In particular, the present invention relates to a vinyl chloride resin composition containing a vinyl chloride copolymer with significantly improved thermal stability.
More specifically, vinyl chloride, or a mixture of one or more monomers capable of copolymerizing vinyl chloride, and bisphenol A-modified diacrylate or bisphenol A-modified dimethacrylate represented by general formula (1) below are copolymerized. This invention relates to a resin composition containing a vinyl chloride-based copolymer that can be obtained by using a polyvinyl chloride copolymer.The molded product obtained from the resin composition can be easily matted, the surface irregularities of the molded product can be very uniform, and the thermal stability is extremely good. be. Vinyl chloride resin is inexpensive, and its molded products have excellent mechanical properties, weather resistance, oil resistance, etc., and are therefore widely used in various fields. (Conventional technology and problems) However, under normal processing conditions, vinyl chloride resin cannot make the surface of the molded product matte.
In addition, lowering the processing temperature or using a large amount of filler to make the product matte has the disadvantage of decreasing mechanical properties, and furthermore, if the process is made matte by embossing or acrylic painting, the molded product will deteriorate. There were inconveniences such as increased costs. However, in recent years, in molded products in various fields,
Matte surfaces with a luxurious feel have come to be preferred, and from the viewpoint of mechanical strength and good tactility, even surface irregularities and fine-grained surfaces have come to be preferred. In order to meet these demands, proposals have already been made to generate gel components during polymerization using crosslinking agents such as diallyl phthalate, diallyl maleate, polyethylene glycol diacrylate, and polyethylene glycol dimethacrylate to obtain a matte surface. However, the vinyl chloride polymers obtained by these techniques have significantly higher thermal stability than ordinary vinyl chloride resins. In the processing of ordinary vinyl chloride resin, it is necessary to use a large amount of heat stabilizer, which increases costs, and changes in processing conditions, such as lowering the processing temperature, can cause Attempts to compensate for the poor stability resulted in problems such as insufficient kneading, resulting in deterioration of the physical properties of the molded product. (Means for solving the problem) In order to improve these drawbacks, as a result of intensive research, we found that bisphenol A represented by the general formula (1) below.
The present inventors have discovered that thermal stability is significantly improved by using modified diacrylates or bisphenol A-modified dimethacrylates, and have completed the present invention. That is, the present invention combines vinyl chloride, or a mixture of one or more monomers copolymerizable with vinyl chloride, and bisphenol A-modified diacrylate or bisphenol A-modified dimethacrylate represented by the following general formula (1). A vinyl chloride copolymer obtained by polymerization,
The contents include a normal vinyl chloride resin or a vinyl chloride resin composition comprising a vinyl chloride resin. (X is a group selected from a hydrogen atom, a methyl group, and a hydroxyl group, and n is an integer of 1 to 80) The main object of the present invention is to use vinyl chloride or a mixture of one or more monomers copolymerizable with vinyl chloride. By using a vinyl chloride copolymer obtained by copolymerizing bisphenol A-modified diacrylate or bisphenol A-modified dimethacrylate represented by the general formula (1) above, the surface unevenness is uniform and the texture is uniform. To provide a vinyl chloride-based resin composition containing a vinyl chloride-based copolymer, from which a molded article with fine texture and good texture and matte finish can be easily obtained. That is, by blending stabilizers, lubricants, antioxidants, rubbers, ultraviolet absorbers, processing aids, pigments, etc. into the resin composition containing the copolymer and processing it, various types of materials in the hard field can be used. By adding a plasticizer to soften the molded products, various molded products in the soft field can be made with uniform surface irregularities.
It is fine-grained, has a good texture, and can be made matte. The reason why the thermal stability of the copolymer obtained by using the bisphenol A-modified diacrylate or the bisphenol A-modified dimethacrylate represented by the general formula (1) is significantly improved is not yet clear. However, since various derivatives of bisphenol A have been added to polyvinyl chloride and the like as heat stabilizers, it is presumed that bisphenol residues have the effect of improving thermal stability. In addition, a gel component is generated by crosslinking by the functional groups at both ends, and the gel component remains in the molded product, resulting in a uniform, fine-grained surface, good texture, and matte finish. The bisphenol A-modified diacrylate or bisphenol A-modified dimethacrylate used in the present invention includes Viscoat #540, Viscoat #700 (manufactured by Osaka Organic Chemical Industry Co., Ltd.), and XD8008.01.
(manufactured by Dow Chemical Company) etc. are commercially available. The vinyl chloride copolymer of the present invention can be produced by suspension polymerization, emulsion polymerization, bulk polymerization, solution polymerization, etc.
Although any conventionally known polymerization method may be used, a suspension polymerization method is preferred from the viewpoint of ease of production and production cost. The amount of the compound used in the present invention is 0.001 parts by weight to 15 parts by weight based on 100 parts by weight of vinyl chloride monomer.
The amount is preferably 0.01 to 5 parts by weight, particularly preferably 0.01 to 5 parts by weight. Further, when adding the compound, the operation of adding it afterward during the polymerization does not impair the object of the present invention. The polymerization temperature in suspension polymerization is not particularly limited, but is preferably from 20°C to 80°C. Further, changing the polymerization temperature during the polymerization does not impair the purpose of the present invention. The initiator used in suspension polymerization may be any initiator that is normally used in the polymerization of vinyl chloride resins, such as lauryl peroxide, di-2-ethylhexyl peroxydicarbonate, isopropyl peroxy Organic peroxides such as dicarbonate, isobutyryl peroxide, 3,5,5-trimethylhexanoyl peroxide, t-butylperoxypivalate, azo radicals such as azobisisobutyronitrile, azobisvaleronitrile, etc. One or more of the initiators can be used. moreover,
The purpose of the present invention is not changed by operations such as adding these initiators midway through the process. Dispersants used in suspension polymerization include partially saponified polyvinyl acetate, methylcellulose, hydroxypropoxymethylcellulose, ethylcellulose, hydroxyethylcellulose, polyvinylpyrrolidone,
Known dispersants such as a copolymer of maleic anhydride and methyl vinyl ether, organic polymer dispersants such as gelatin, casein, and starch, and inorganic dispersants such as talc, calcium sulfate, and calcium phosphate can be used alone or in combination. . Furthermore, the object of the present invention is not impaired even if such operations as post-addition of these dispersants during polymerization are performed. In the present invention, the monomer forming the main chain is vinyl chloride alone or a mixture of at least 50% by weight of vinyl chloride and a vinyl monomer copolymerizable therewith. Monomers copolymerizable with vinyl chloride include vinyl esters such as vinyl acetate,
Examples include vinyl ethers such as methyl vinyl ether, acrylic acid or methacrylic acid and its esters, maleic acid or fumaric acid and its esters or anhydrides, aromatic vinyl compounds, vinylidene halides, and vinyl monomers such as monoolefins. Ru. In addition, in the present invention, there is no problem in performing operations such as adding these monomers midway, and depending on the reactivity ratio of these monomers, the final molecule This can be done depending on the design. Furthermore, in the present invention, addition of various additives, such as antioxidants, ultraviolet absorbers, heat stabilizers, lubricants, rubbers, etc., which are usually used to modify vinyl chloride resin, or polymerization and Addition of a buffer, etc. to ensure stability does not change the gist of the present invention in any way and can be employed as appropriate depending on the purpose. The copolymer in the composition of the present invention can be used in both hard and soft fields. That is, by blending rubbers, stabilizers, lubricants, antioxidants, ultraviolet absorbers, processing aids, pigments, etc. with the copolymer and processing it, molded articles for hard applications are obtained. Further, by using the copolymer in combination with an ordinary vinyl chloride resin or vinyl chloride resin to obtain a resin composition containing the copolymer, the properties of the copolymer can be fully exhibited. Rubbers that can be used in the present invention include:
Examples include NBR, EPDM, SBR, silicone rubber, natural rubber, polybutadiene, neoprene rubber, isoprene rubber, MBS, EVA, etc. As the stabilizer, one type or a combination of two or more of tin type stabilizers, lead type stabilizers, metal soaps, Ca-Zn type stabilizers, Ba type stabilizers, etc. are used. As the lubricant, one or more of polyethylene wax-based lubricants, stearic acid-based lubricants, alcohol-based lubricants, etc. are used in combination. The elastic vinyl chloride resin used in the present invention is a copolymer containing at least 50% by weight of vinyl chloride, such as a copolymer with vinyl esters such as vinyl acetate, methyl vinyl ether, etc. Copolymers with vinyl ethers of , copolymers with vinyl monomers such as vinylidene halide or monoolefin, and the like. Furthermore, by adding a plasticizer to the copolymer, it is also possible to obtain soft molded products. The amount of plasticizer that can be used is not particularly limited, and may be adjusted as necessary. Furthermore, the plasticizer used is not particularly limited, and one or two of commonly used phthalic acid plasticizers, epoxy plasticizers, phosphate ester plasticizers, polyester plasticizers, etc. More than one species can be used together. (Effects of the Invention) When the vinyl chloride resin composition containing the vinyl chloride copolymer of the present invention is made into a molded article, it is easily matted, and the surface irregularities of the molded article are very uniform.
Further, as shown in the Examples, the resin composition of the present invention is industrially excellent since it exhibits an effect of excellent thermal stability. (Example) Next, embodiments of the present invention will be further clarified by Examples, but these are not intended to limit the scope of the present invention. Reference Examples 1 to 8 In a stainless steel polymerization vessel with an internal volume of 300, 200 parts of ion-exchanged water, 0.2 parts of partially saponified polyvinyl acetate, 0.06 parts of diisopropyl peroxide, 0.06 parts of di-2-ethylhexyl peroxydicarbonate, and 100 parts of vinyl chloride monomer. Viscoat #540 or Viscoat #700 was added in the amounts shown in Table 1 and polymerized at a polymerization temperature of 35° C. for 15 hours. The obtained slurry was dehydrated, dried in a hot air dryer at 5° C. for 18 hours, and used for each measurement. Comparative Examples 1 to 6 In the same manner as in Reference Examples, predetermined amounts of ion-exchanged water, partially saponified polyvinyl acetate, diisopropyl peroxide, di-2-ethylhexyl peroxydicarbonate, vinyl chloride monomer, and the crosslinking agent shown in Table 1 were added. Polymerization was carried out at a charging polymerization temperature of 35°C for 15 hours. It was dried in the same manner as in the reference example and used for each measurement. In addition, each physical property value was measured as follows. (1) Preparation of test piece: Blend Sample copolymer 100 parts by weight Dioctyl phthalate 100 Tribasic lead sulfate 3 Lead stearate 1 Calcium carbonate 30 Blend the mixture at a roll temperature of 185℃. Knead for 10 minutes to produce a masticated sheet with a thickness of approximately 0.7 m/m, and press at a pressing temperature of 190°C.
A sample sheet for measurement was prepared by press molding at a pressure of 200 kg/cm 2 . (2) Compression set: In accordance with JIS-K6301, the compression conditions were a compression ratio of 25% and a temperature of 70°C for 22 hours. (3) Tensile strength: A test piece was punched out from a press-formed sheet in accordance with JIS-K6723, and measured using a tensile tester at a measurement temperature of 25°C and a tensile speed of 200 mm/min. (4) HC1 removal rate: Automatic titrator AT-
107 (manufactured by Kyoto Denshi Kogyo Co., Ltd.) at an oil bath temperature of 235°C, a N 2 flow rate of 20 ml/min, and a titration rate of 0.02 ml/min.
After placing 10g of the sample (masticated sheet cut into approximately 3mm2 pieces) in an oil bath,
The time required for the amount of NaOH solution used to reach 5.0 ml was determined.

【表】【table】

【表】 表−1より該共重合体を軟質化した時には、圧
縮永久歪、抗張力のバランスは良くなり、かつ脱
HC1速度が極端に長くなつており、熱安定性が
著しく向上している事が判る。 実施例1〜8、比較例7〜14 参考例3及び参考例7で得られた共重合体、比
較例2及び比較例5で得られた共重合体と、塩化
ビニルホモポリマー(700)又は塩化ビニル酢
酸ビニル共重合体(VAc含量8%、700)を表
−2に示すブレンド比率にて、全樹脂に対してス
ズ安定剤2部、ステアリン酸0.5部、顔料0.5部を
配合し、ロール温度180℃で7分間混練し、0.6mm
厚のシートを得た。ロールシートを表面状態を目
視によつて評価し、結果を表−2に示した。
[Table] From Table 1, when the copolymer is softened, the balance between compression set and tensile strength becomes better, and
It can be seen that the HC1 speed has become extremely long, indicating that the thermal stability has been significantly improved. Examples 1 to 8, Comparative Examples 7 to 14 The copolymers obtained in Reference Examples 3 and 7, the copolymers obtained in Comparative Examples 2 and 5, and vinyl chloride homopolymer (700) or Vinyl chloride vinyl acetate copolymer (VAc content 8%, 700) was blended with 2 parts of tin stabilizer, 0.5 part of stearic acid, and 0.5 part of pigment to the total resin at the blend ratio shown in Table 2, and then rolled. Knead for 7 minutes at a temperature of 180℃, 0.6mm
A thick sheet was obtained. The surface condition of the roll sheet was visually evaluated and the results are shown in Table 2.

【表】 表−2の結果より、艶消状態は比較例とほとん
ど同等ではあるが、表面凹凸状態が良好になり、
かつG.O黒化時間が大巾に改良されている事が判
る。尚、G.O黒化時間は次の様な条件にて測定し
た。 実施例1〜8、比較例7〜14で得られたシート
を3cm×6cmに切断し、あらかじめ200℃の雰囲
気に加熱設定されたギヤー式老化試験機の中に入
れ、15分毎にシートを取り出し、シート片の着色
程度を肉眼で観察し、黒く着色するまでの時間を
求めた。
[Table] From the results in Table 2, the matte state is almost the same as the comparative example, but the surface unevenness is improved.
It can also be seen that the GO blackening time has been greatly improved. The GO blackening time was measured under the following conditions. The sheets obtained in Examples 1 to 8 and Comparative Examples 7 to 14 were cut into 3 cm x 6 cm pieces, placed in a gear type aging tester preheated to an atmosphere of 200°C, and the sheets were cut every 15 minutes. The sheet piece was taken out, and the degree of coloring of the sheet piece was observed with the naked eye, and the time required for the sheet piece to become black was determined.

Claims (1)

【特許請求の範囲】 1 塩化ビニル、又は更に塩化ビニルと共重合可
能な単量体1種以上の混合物と下記一般式(1)で示
されるビスフエノールA変性ジアクリレート又は
ビスフエノールA変性ジメタクリレート(塩化ビ
ニル系単量体100重量部に対し、0.001〜15重量
部)とを共重合してなる塩化ビニル系共重合体
と、通常の塩化ビニル樹脂又は、塩化ビニル系樹
脂とからなる塩化ビニル系樹脂組成物。 (Xは水素原子、メチル基、水酸基から選ばれる
基、nは1〜80の整数を表わす。)
[Scope of Claims] 1. Vinyl chloride, or a mixture of one or more monomers copolymerizable with vinyl chloride, and bisphenol A-modified diacrylate or bisphenol A-modified dimethacrylate represented by the following general formula (1). (0.001 to 15 parts by weight based on 100 parts by weight of vinyl chloride monomer), and a vinyl chloride copolymer formed by copolymerizing a vinyl chloride-based copolymer with a normal vinyl chloride resin or a vinyl chloride-based resin. based resin composition. (X represents a group selected from a hydrogen atom, a methyl group, and a hydroxyl group, and n represents an integer from 1 to 80.)
JP17274785A 1985-08-06 1985-08-06 Vinyl chloride resin composition containing vinyl chloride copolymer Granted JPS6143645A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17274785A JPS6143645A (en) 1985-08-06 1985-08-06 Vinyl chloride resin composition containing vinyl chloride copolymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17274785A JPS6143645A (en) 1985-08-06 1985-08-06 Vinyl chloride resin composition containing vinyl chloride copolymer

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP56082862A Division JPS57195711A (en) 1981-05-29 1981-05-29 Vinyl chloride copolymer and composition thereof

Publications (2)

Publication Number Publication Date
JPS6143645A JPS6143645A (en) 1986-03-03
JPH0157138B2 true JPH0157138B2 (en) 1989-12-04

Family

ID=15947571

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17274785A Granted JPS6143645A (en) 1985-08-06 1985-08-06 Vinyl chloride resin composition containing vinyl chloride copolymer

Country Status (1)

Country Link
JP (1) JPS6143645A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005281567A (en) * 2004-03-30 2005-10-13 Kaneka Corp Vinyl chloride resin composition for calendering
JP2005281570A (en) * 2004-03-30 2005-10-13 Kaneka Corp Vinyl chloride resin composition for injection-molded article
JP2005281571A (en) * 2004-03-30 2005-10-13 Kaneka Corp Hard vinyl chloride resin composition for extrusion
WO2005097889A1 (en) * 2004-03-30 2005-10-20 Kaneka Corporation Vinyl chloride resin composition
JP2005281569A (en) * 2004-03-30 2005-10-13 Kaneka Corp Vinyl chloride-based resin composition

Also Published As

Publication number Publication date
JPS6143645A (en) 1986-03-03

Similar Documents

Publication Publication Date Title
JPS6144883B2 (en)
AU610013B2 (en) Flexible blend compositions based on overpolymers of vinyl chloride polymers on ethylene copolymers
JPH0157138B2 (en)
US5055515A (en) Flexible overpolymers of vinyl chloride polymers on ethylene copolymers
JPS6312089B2 (en)
US4179481A (en) Vinyl chloride resin compositions
JPS63309549A (en) Vinyl chloride resin composition
JPH0149728B2 (en)
JP2531747B2 (en) Rubber composition
JPH08134142A (en) Production of matte vinyl chloride-based polymer and production of composition of the same polymer
US4972012A (en) Polyvinyl chloride resin composition
JPS58127717A (en) Production of vinyl chloride graft copolymer
JPH07188488A (en) Polyvinyl chloride resin composition
JPH0782332A (en) Block copolymer and resin composition containing the same
JPS61221209A (en) Production of vinyl chloride resin
JPH09208631A (en) Vinyl chloride polymer
JPS6251965B2 (en)
JPH085924B2 (en) Method for producing vinyl chloride copolymer
JPH02182741A (en) Vinyl chloride resin composition
JPH02269709A (en) Production of vinyl chloride copolymer
JPH0374438A (en) Matte heat-shrinkable film
JPH0529641B2 (en)
JPS6249902B2 (en)
JPH0660224B2 (en) Method for producing vinyl chloride resin
JPH03244613A (en) Production of vinyl chloride polymer