JPH0570663B2 - - Google Patents
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- Publication number
- JPH0570663B2 JPH0570663B2 JP59076443A JP7644384A JPH0570663B2 JP H0570663 B2 JPH0570663 B2 JP H0570663B2 JP 59076443 A JP59076443 A JP 59076443A JP 7644384 A JP7644384 A JP 7644384A JP H0570663 B2 JPH0570663 B2 JP H0570663B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- polyvinyl chloride
- parts
- graft copolymer
- plasticizer
- 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 - Lifetime
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- Compositions Of Macromolecular Compounds (AREA)
Description
本発明はポリ塩化ビニルと高分子可塑剤からな
る加工性の良好な塩化ビニル系樹脂組成物に関す
る。
塩化ビニル樹脂はすぐれた物理的、機械的性質
を有しているため、硬質、半硬質、軟質等多くの
用途がある。
低温から常温において柔軟で弾性を有する塩化
ビニル樹脂成形品を得るために、一般に塩化ビニ
ル樹脂にフタル酸エステル、トリメリツト酸エス
テル、ポリエステル系等の可塑剤を配合して使用
する。中でも耐油性、耐抽出性に優れた軟質ポリ
塩化ビニル組成物を得ようとする場合、分子量
10000以上の高分子可塑剤を用いて外部可塑化す
ることがフタル酸エステル等の低分子可塑剤を用
いて外部可塑化することに比べて耐油性、耐抽出
性で優れているので好ましい。
ところで、通常の懸濁重合法により得られるポ
リ塩化ビニルに、かかる高分子可塑剤を配合した
場合、混練時のゲル化特性の悪化がひき起こされ
るという問題がある。
これは、重合時に用いられた分散剤により粒子
表面に皮膜を生じているために、この皮膜が障壁
となつて可塑剤の吸収を妨げ、混練時のゲル化特
性の悪化が生じるものと推定される。かかる傾向
は分子量10000以上の高分子可塑剤において著し
い。皮膜の少ないポリ塩化ビニル、即ち、塩化ビ
ニルを水性媒体で懸濁重合するに当たり(a)親油性
のソルビタン高級脂肪酸エステルおよび/また
は、親油性のポリオキシエチレンソルビタン高級
脂肪酸エステル存在下に重合を開始し、(b)その重
合転化率が5〜40%に達した時点で水溶性セルロ
ーズ誘導体を添加して製造されるポリ塩化ビニル
は、分子量10000以上の高分子可塑剤と混練する
ことにより、ゲル化特性は向上することが知られ
ている(特開昭58−168644号)が、実際の生産機
ではバンバリーミキサーのような練りの強い機械
を必要とする。
しかし、この様な練りの強い機械で混練すると
熱劣化が激しくなり、製品が着色するという問題
が生じる。
又、二本ロールや押出機等の練りの弱い混練機
を用いることのような問題は解消されるのである
が、実際は混練不足によるブツが残るという問題
があり、更なる樹脂組成物の改良が望まれてい
る。
本発明者らは、二本ロールや押出機等の練りの
弱い混練機でもゲル化特性に優れた塩化ビニル系
樹脂組成物を得るために鋭意研究した結果、ポリ
塩化ビニルと分子量10000以上の高分子可塑剤と
を混練するに当り、更にポリ塩化ビニルに他のモ
ノマーをグラフト共重合体したグラフト共重合体
を添加しなならば、おどろく程ゲル化特性が向上
することを見出し、本発明を完成した。
すなわち、本発明は、ポリ塩化ビニル100重量
部、高分子可塑剤25〜200重量部、およびポリ塩
化ビニル99.5〜70重量%に酢酸ビニル、アクリル
酸ブチル、メタクリル酸メチル、ヘキセン−1及
びスチレンのうち少なくとも1種類以上のコモノ
マー0.5〜30重量%をグラフト共重合させたグラ
フト共重合体2〜150重量部とからなることを特
徴とする加工性の良好な塩化ビニル系樹脂組成物
である。
本発明に用いられるポリ塩化ビニルとは、塩化
ビニルの単独重合体であり、例えばソルビタン高
級脂肪酸エステル、ポリオキシエチレンソルビタ
ン高級脂肪酸エステル、水溶性セルローズ誘導
体、ポリビニルアルコール、ポリビニルピロリド
ン、ゼラチン等を分散剤として併用し、触媒とし
て、例えばベンゾイルパーオキサイド、ラウロイ
ルパーオキサイド、カプロイルパーオキサイド、
ジイソプロピルパーオキシジカーボネート、ジ
(2−エチルヘキシル)パーオキシジカーボネー
ト、ターシヤリブチルパーオキシビバレート等の
有機過酸化物;2,2′−アゾビスイソブチロニト
リル、2,2′−アゾビス−2,4−ジメチルバレ
ロニトリル、2,2′−アゾビス−4−メトキシ−
2,4−ジメチルバレロニトリル等のアゾ化合物
を単独又は組み合わせて使用して、塩化ビニルを
重合して得られたものが好適である。
本発明に用いられる高分子可塑剤としては、ポ
リエステル系高分子可塑剤、エチレン・ビニルア
セテート系高分子可塑剤、エチレン・ビニルアセ
テート・一酸化炭素の共重合体からなる高分子可
塑剤等の高分子可塑剤、およびこれらの変性物が
あげられる。なお、ブリードなどの問題から分子
量10000以上のものが望ましい。中でもエチレ
ン・ビニルアセテート・一酸化炭素の共重合体か
らなる分子量10000以上の高分子可塑剤は特に耐
油性、耐抽出性を有するポリ塩化ビニル組成物を
得る場合に有効である。
高分子可塑剤の配合量は、ポリ塩化ビニル100
重量部に対して25〜500重量部が望ましい。25重
量部未満では可塑化効果がほとんどなく、また
500重量部を超えて用いるとポリ塩化ビニルの特
質が損なわれるので好ましくない。
本発明において添加される塩化ビニルグラフト
共重合体は、ポリ塩化ビニルに酢酸ビニル、アク
リル酸ブチル、メタクリル酸メチル、ヘキセン−
1及びスチレンのうち少なくとも1種類以上のコ
モノマーをグラフト共重合させたグラフト共重合
体である。
またグラフト共重合体中のこれらのモノマーの
量は0.5〜30重量%であり、この範囲をはずれた
ものでは、本発明の効果は得られない。
なお、幹ポリマーとしてのポリ塩化ビニルは、
重合度200〜2000好ましくは400〜1500のものが好
適に用いられる。
塩化ビニルグラフト共重合体の配合量は、ポリ
塩化ビニル100重量部に対して、2〜150重量部が
望ましい。この範囲をはずれると本発明の効果は
得られない。
本発明の組成物は、ポリ塩化ビニル、塩化ビニ
ルグラフト共重合体及び高分子可塑剤に、必要に
応じて、安定剤、滑剤、発泡剤、充填剤、紫外線
吸収剤、顔料、レベリング剤、導電性カーボン、
難燃剤等の添加剤を加えて、ヘンシエルミキサ
ー、リボンブレンダー等の公知の装置で混合して
得られる。
又、混練装置としては、練りの強いバンバリー
ミキサーから、練りの弱い二本ロールや押出機等
まで使用することができ、カレンダー、溶融押出
し、スタンプ、インジエクシヨン等の公知の方法
により成形加工されて実用に供される。
本発明の組成物は、成形されたときに未ゲル化
粒子が少ないのでなめらかな表面を有し、医療
用、産業用、食品用に好適に使用される。
以下実施例により、本発明を説明する。
実施例 1
内容積3000のオートクレーブに純水1200Kg、
ヒドロキシプロピルメチルセルローズ1.2Kg、重
合度800のポリ塩化ビニル600Kg、α,α′−アゾビ
スイソブチロニトリル3.0Kgを入れ、内部の空気
を窒素で置換した後に、酢酸ビニル70Kgを装入し
た。80℃で10時間反応させた後、反応生成物から
未反応モノマーを除去し、これを脱水乾燥して、
粉末状のグラフト共重合体樹脂を得た。このグラ
フト共重合体樹脂は、分析の結果塩化ビニル以外
の成分は10%であつた。
このグラフト共重合体樹脂を第1表に示した割
合で、重合度1050のポリ塩化ビニルに高分子可塑
剤及びCa−Ba系複合安定剤と共に配合してロー
ルシートを作成し、ゲルレベルを評価した。
実施例 2〜9
実施例1の重合度800のポリ塩化ビニルに代え、
第1表に示した重合度のポリ塩化ビニルを使用
し、酢酸ビニル70Kgに代え、第1表に示したコモ
ノマーを使用し、コモノマーの重合量が第1表に
示した含有量になる様に実施例1と同様のグラフ
ト共重合を行ない、グラフト共重合樹脂を得た。
以下、実施例1と同様にしてゲルレベル評価し
た。
比較例 1〜12
第1表に示した割合で、重合度1050のポリ塩化
ビニル、塩化ビニルグラフト共重合体、高分子可
塑剤及びCa−Ba系複合安定剤を配合してロール
シートを作成し、ゲルレベルを評価した。
ゲルテストは160℃の8インチロールで約0.3mm
厚にて、10分間混練し、シートとしてとり出し
(10cm×10cm)の四角中にある未溶融のポリ塩化
ビニル粒子を目視により計数した。単位は個数。
これらの測定結果を第1表に示す。
TECHNICAL FIELD The present invention relates to a vinyl chloride resin composition comprising polyvinyl chloride and a polymer plasticizer and having good processability. Vinyl chloride resin has excellent physical and mechanical properties, so it has many uses such as hard, semi-hard, and soft. In order to obtain vinyl chloride resin molded articles that are flexible and elastic at low to room temperatures, vinyl chloride resin is generally mixed with a plasticizer such as a phthalate ester, a trimellitic acid ester, or a polyester type plasticizer. Among them, when trying to obtain a soft polyvinyl chloride composition with excellent oil resistance and extraction resistance, the molecular weight
External plasticization using a polymeric plasticizer of 10,000 or more is preferable because it is superior in oil resistance and extraction resistance compared to external plasticization using a low molecular plasticizer such as phthalate ester. By the way, when such a polymer plasticizer is blended with polyvinyl chloride obtained by a normal suspension polymerization method, there is a problem in that gelling properties during kneading are deteriorated. This is thought to be because the dispersant used during polymerization forms a film on the particle surface, which acts as a barrier and prevents the absorption of plasticizer, resulting in deterioration of gelling properties during kneading. Ru. This tendency is remarkable in polymer plasticizers with a molecular weight of 10,000 or more. When polyvinyl chloride with a small film, that is, vinyl chloride, is suspended polymerized in an aqueous medium, (a) polymerization is initiated in the presence of lipophilic sorbitan higher fatty acid ester and/or lipophilic polyoxyethylene sorbitan higher fatty acid ester. (b) When the polymerization conversion rate reaches 5 to 40%, polyvinyl chloride produced by adding a water-soluble cellulose derivative is kneaded with a polymeric plasticizer having a molecular weight of 10,000 or more to form a gel. It is known that the chemical properties can be improved (Japanese Patent Application Laid-Open No. 168644/1982), but in actual production, a machine with strong kneading power such as a Banbury mixer is required. However, when kneading with such a strong kneading machine, thermal deterioration becomes severe and the problem arises that the product becomes discolored. In addition, although this solves the problem of using a kneading machine with weak kneading properties such as a two-roll machine or an extruder, there is actually a problem that lumps remain due to insufficient kneading, and further improvement of the resin composition is required. desired. The present inventors have conducted intensive research to obtain a vinyl chloride resin composition that has excellent gelation properties even with weak kneading machines such as two rolls and extruders. When kneading with a molecular plasticizer, it was discovered that if a graft copolymer obtained by grafting polyvinyl chloride with other monomers was added, the gelling properties would be surprisingly improved, and the present invention was realized. completed. That is, the present invention includes 100 parts by weight of polyvinyl chloride, 25 to 200 parts by weight of a polymeric plasticizer, and 99.5 to 70 parts by weight of polyvinyl chloride, vinyl acetate, butyl acrylate, methyl methacrylate, hexene-1, and styrene. This is a vinyl chloride resin composition with good processability, characterized by comprising 2 to 150 parts by weight of a graft copolymer obtained by graft copolymerizing 0.5 to 30 weight % of at least one type of comonomer. The polyvinyl chloride used in the present invention is a homopolymer of vinyl chloride, and for example, sorbitan higher fatty acid ester, polyoxyethylene sorbitan higher fatty acid ester, water-soluble cellulose derivative, polyvinyl alcohol, polyvinylpyrrolidone, gelatin, etc. are used as a dispersing agent. For example, benzoyl peroxide, lauroyl peroxide, caproyl peroxide,
Organic peroxides such as diisopropyl peroxydicarbonate, di(2-ethylhexyl) peroxydicarbonate, tertiary butyl peroxybivalate; 2,2'-azobisisobutyronitrile, 2,2'-azobis- 2,4-dimethylvaleronitrile, 2,2'-azobis-4-methoxy-
Preferably, it is obtained by polymerizing vinyl chloride using an azo compound such as 2,4-dimethylvaleronitrile alone or in combination. Examples of polymer plasticizers used in the present invention include polyester polymer plasticizers, ethylene-vinyl acetate-based polymer plasticizers, and polymer plasticizers made of ethylene-vinyl acetate-carbon monoxide copolymers. Mention may be made of molecular plasticizers and modified products thereof. Note that it is desirable to have a molecular weight of 10,000 or more due to problems such as bleeding. Among them, a polymer plasticizer having a molecular weight of 10,000 or more and consisting of a copolymer of ethylene, vinyl acetate, and carbon monoxide is particularly effective in obtaining a polyvinyl chloride composition having oil resistance and extraction resistance. The amount of polymer plasticizer blended is polyvinyl chloride 100
25 to 500 parts by weight is desirable. If it is less than 25 parts by weight, there is almost no plasticizing effect, and
If it is used in an amount exceeding 500 parts by weight, the properties of polyvinyl chloride will be impaired, which is not preferable. The vinyl chloride graft copolymer added in the present invention includes polyvinyl chloride, vinyl acetate, butyl acrylate, methyl methacrylate, hexene-
This is a graft copolymer obtained by graft copolymerizing at least one comonomer of 1 and styrene. Further, the amount of these monomers in the graft copolymer is 0.5 to 30% by weight, and if it is outside this range, the effects of the present invention cannot be obtained. In addition, polyvinyl chloride as the backbone polymer is
Those having a degree of polymerization of 200 to 2,000, preferably 400 to 1,500 are suitably used. The blending amount of the vinyl chloride graft copolymer is preferably 2 to 150 parts by weight based on 100 parts by weight of polyvinyl chloride. Outside this range, the effects of the present invention cannot be obtained. The composition of the present invention includes polyvinyl chloride, a vinyl chloride graft copolymer, and a polymeric plasticizer, as well as a stabilizer, a lubricant, a blowing agent, a filler, an ultraviolet absorber, a pigment, a leveling agent, and a conductive agent, as necessary. carbon,
It is obtained by adding additives such as flame retardants and mixing in a known device such as a Henschel mixer or a ribbon blender. In addition, kneading equipment can range from a Banbury mixer with strong kneading to a two-roll machine or extruder with weak kneading, and can be molded and processed by known methods such as calendaring, melt extrusion, stamping, and injection molding. served. When the composition of the present invention is molded, it has a smooth surface due to the small amount of ungelled particles, and is suitable for use in medical, industrial, and food applications. The present invention will be explained below with reference to Examples. Example 1 1200 kg of pure water in an autoclave with an internal volume of 3000,
1.2 kg of hydroxypropyl methyl cellulose, 600 kg of polyvinyl chloride with a degree of polymerization of 800, and 3.0 kg of α,α'-azobisisobutyronitrile were charged, and after replacing the air inside with nitrogen, 70 kg of vinyl acetate was charged. After reacting at 80°C for 10 hours, unreacted monomers were removed from the reaction product, which was dehydrated and dried.
A powdered graft copolymer resin was obtained. As a result of analysis, this graft copolymer resin contained 10% of components other than vinyl chloride. This graft copolymer resin was blended with polyvinyl chloride having a degree of polymerization of 1050 along with a polymer plasticizer and a Ca-Ba composite stabilizer in the proportions shown in Table 1 to prepare a roll sheet, and the gel level was evaluated. . Examples 2 to 9 In place of polyvinyl chloride with a degree of polymerization of 800 in Example 1,
Use polyvinyl chloride with the polymerization degree shown in Table 1, replace 70 kg of vinyl acetate with the comonomer shown in Table 1, and adjust the polymerization amount of the comonomer to the content shown in Table 1. Graft copolymerization was carried out in the same manner as in Example 1 to obtain a graft copolymer resin. Hereinafter, the gel level was evaluated in the same manner as in Example 1. Comparative Examples 1 to 12 A roll sheet was prepared by blending polyvinyl chloride with a degree of polymerization of 1050, a vinyl chloride graft copolymer, a polymer plasticizer, and a Ca-Ba composite stabilizer in the proportions shown in Table 1. , the gel level was evaluated. Gel test is approximately 0.3mm with 8 inch roll at 160℃
The mixture was kneaded for 10 minutes, and a sheet was taken out and the unmelted polyvinyl chloride particles in a square (10 cm x 10 cm) were visually counted. The unit is the number of pieces. The results of these measurements are shown in Table 1.
【表】
実施例10〜12及び比較例13〜15
重合度1300のポリ塩化ビニルに第2表に示した
割合で実施例3で得た塩化ビニルグラフト共重合
体、高分子可塑剤及びCa−Ba系複合安定剤を配
合し、実施例1と同様にして、ゲルレベルを評価
した。これらの測定結果を第2表に示す。[Table] Examples 10 to 12 and Comparative Examples 13 to 15 The vinyl chloride graft copolymer obtained in Example 3, a polymer plasticizer, and Ca- A Ba-based composite stabilizer was blended, and the gel level was evaluated in the same manner as in Example 1. The results of these measurements are shown in Table 2.
【表】
実施例 13
重合度1050のポリ塩化ビニルの代わりに重合度
2800のポリ塩化ビニルを使用した以外は実施例1
と同様にしてゲルレベルを評価した結果90個であ
つた。
比較例 16
重合度1050のポリ塩化ビニルの代わりに重合度
2800のポリ塩化ビニルを使用した以外は、比較例
10と同様にしてゲルレベルを評価した結果、800
個であつた。
比較例のポリ塩化ビニル又は、塩化ビニルグラ
フト共重合体の単独もしくは塩化ビニル共重合体
の1重量部未満もしくは150重量部以上ではゲル
レベルは100個以上であるが、本発明である実施
例ではいずれも100個未満となり優れていた。[Table] Example 13 Polymerization degree instead of polyvinyl chloride with a polymerization degree of 1050
Example 1 except that 2800 polyvinyl chloride was used.
The gel level was evaluated in the same manner as above, and the result was 90 pieces. Comparative Example 16 Polymerization degree instead of polyvinyl chloride with a polymerization degree of 1050
Comparative example except that 2800 PVC was used.
As a result of evaluating the gel level in the same manner as in 10, it was found to be 800
It was individual. Comparative examples of polyvinyl chloride, vinyl chloride graft copolymers alone, or vinyl chloride copolymers of less than 1 part by weight or more than 150 parts by weight have a gel level of 100 or more, but in the examples of the present invention, none It was also excellent, with less than 100 pieces.
Claims (1)
〜500重量部、およびポリ塩化ビニル99.5〜70重
量%に酢酸ビニル、アクリル酸ブチル、メタクリ
ル酸メチル、ヘキセン−1及びスチレンのうち少
なくとも1種類以上のコモノマー0.5〜30重量%
をグラフト共重合させたグラフト共重合体2〜
150重量部とからなることを特徴とする加工性の
良好な塩化ビニル系樹脂組成物。1 100 parts by weight of polyvinyl chloride, 25 parts by weight of polymer plasticizer
~500 parts by weight, and 99.5-70% by weight of polyvinyl chloride and 0.5-30% by weight of at least one comonomer selected from vinyl acetate, butyl acrylate, methyl methacrylate, hexene-1, and styrene.
Graft copolymer 2 ~
150 parts by weight of a vinyl chloride resin composition with good processability.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7644384A JPS60221447A (en) | 1984-04-18 | 1984-04-18 | Vinyl chloride resin composition of good processability |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7644384A JPS60221447A (en) | 1984-04-18 | 1984-04-18 | Vinyl chloride resin composition of good processability |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60221447A JPS60221447A (en) | 1985-11-06 |
| JPH0570663B2 true JPH0570663B2 (en) | 1993-10-05 |
Family
ID=13605291
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7644384A Granted JPS60221447A (en) | 1984-04-18 | 1984-04-18 | Vinyl chloride resin composition of good processability |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60221447A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60173036A (en) * | 1984-02-17 | 1985-09-06 | Nippon Zeon Co Ltd | Method for producing vinyl chloride resin composition |
-
1984
- 1984-04-18 JP JP7644384A patent/JPS60221447A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60221447A (en) | 1985-11-06 |
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