JPS6140326A - Method of blending polyvinyl chloride with high polymer plasticizer - Google Patents

Method of blending polyvinyl chloride with high polymer plasticizer

Info

Publication number
JPS6140326A
JPS6140326A JP15919284A JP15919284A JPS6140326A JP S6140326 A JPS6140326 A JP S6140326A JP 15919284 A JP15919284 A JP 15919284A JP 15919284 A JP15919284 A JP 15919284A JP S6140326 A JPS6140326 A JP S6140326A
Authority
JP
Japan
Prior art keywords
polyvinyl chloride
kneading
plasticizer
polymer plasticizer
high polymer
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.)
Granted
Application number
JP15919284A
Other languages
Japanese (ja)
Other versions
JPH0522729B2 (en
Inventor
Takashi Isaka
井坂 孝
Tadashi Kasuga
春日 廉
Hideyuki Itagaki
板垣 秀行
Takeshi Harigai
針谷 武
Masahito Yoshida
将人 吉田
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP15919284A priority Critical patent/JPS6140326A/en
Publication of JPS6140326A publication Critical patent/JPS6140326A/en
Publication of JPH0522729B2 publication Critical patent/JPH0522729B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:In kneading polyvinyl chloride with a high polymer plasticizer, to obtain a kneaded resin for medical uses, having improved transparency, free from ungelatinized particles even by the use of a blender having low kneading power such as an extruder, etc., by blending the polyvinyl chloride with the high polymer plasticizer dividedly, kneading them. CONSTITUTION:In kneading polyvinyl chloride with a high polymer plasticizer (ethylene vinyl acetate carbon monoxide copolymer having preferably >=10,000 mol.wt.), the polyvinyl chloride is blended with part of the high polymer plasticizer (preferably 10-40pts.wt. plasticizer based on 100pts.wt. polyvinyl chloride resin), kneaded, and the blend in blended with the rest of the plasticizer and kneaded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ポリ塩化ビニルと高分子可塑剤からなる未ゲ
ル分のないペレットの混練方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for kneading pellets containing polyvinyl chloride and a polymeric plasticizer and having no ungelled content.

〔従来の技術〕[Conventional technology]

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。
Vinyl chloride resin has excellent physical and mechanical properties, so it has many uses such as hard, semi-hard, and soft.

低温から常温において柔軟で弾性を有する塩′化ビニル
樹脂成型品を得るためには、一般に塩化ビニル樹脂にフ
タル酸エステル、トリメリット酸エステル、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10.000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望ましい。
In order to obtain vinyl chloride resin molded products that are flexible and elastic at low to room temperatures, vinyl chloride resin is generally mixed with a plasticizer such as phthalate ester, trimellitate ester, or polyester. Above all, when trying to obtain a soft polyvinyl chloride composition with excellent oil resistance and extraction resistance, external plasticization using a polymer plasticizer with a molecular weight of 10,000 or more is recommended. It is desirable because it has superior oil resistance and extraction resistance compared to external plasticization using a chemical agent.

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すると混練不良が生
じるという問題がある。
By the way, when such a polymer plasticizer is blended with polyvinyl chloride obtained by a normal suspension polymerization method, there is a problem that poor kneading occurs.

これは、ポリ塩化ビニルが粒子表面に皮膜を生じている
ためであり、この皮膜が障壁となって可塑剤の吸収を妨
げ、混練時のゲル化特性が悪化しているものと推定され
る。かかる傾向は分子量10.000以上の高分子可塑
剤を配合する場合において著しい。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、親水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10,000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(特開昭58−16864
4号)が、実際はバンバリーミキサ−のような練りの強
い機械を必要とする。
This is because polyvinyl chloride forms a film on the particle surface, and it is presumed that this film acts as a barrier and prevents absorption of the plasticizer, thereby deteriorating the gelation properties during kneading. This tendency is remarkable when a polymer plasticizer with a molecular weight of 10,000 or more is blended. 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 hydrophilic 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 can be produced by kneading it with a polymeric plasticizer having a molecular weight of 10,000 or more. , the gelling properties are improved (Japanese Patent Application Laid-Open No. 16864/1986)
No. 4) actually requires a strong mixing machine such as a Banbury mixer.

しかし、この様な練りの強い機械で混練すると樹脂の熱
劣化が激しくなり、製品が着色するという問題が生じる
However, kneading with such a strong kneading machine causes severe thermal deterioration of the resin, causing the problem that the product becomes discolored.

又、二本ロールや押出機等の練りの弱い混練機を用いる
とこの製品が着色する問題は解消されるのであるが、実
際は混練不足によるブッが残るという問題があった。
Furthermore, if a kneading machine with a weak kneading capacity such as a two-roll machine or an extruder is used, the problem of coloring of the product can be solved, but in reality, there is a problem that a lump remains due to insufficient kneading.

この問題点を改良する方法として、ポリ塩化ビニルと高
分子可塑剤に更に塩化ビニル共重合体を添加し混練する
方法を提案した(特願昭59−076442.59−0
76443.59−076444 )。
As a method to improve this problem, we proposed a method in which a vinyl chloride copolymer is further added to polyvinyl chloride and a polymeric plasticizer and kneaded (Patent Application No. 59-076442.59-0
76443.59-076444).

この方法で混練すると、ゲル化特性は改良されるが、塩
化ビニル共重合体自体透明性に劣るため、透明配合では
透明性が不充分となり、使用上制限されるという欠点を
有しており、更に改良が望まれていた。
Kneading by this method improves the gelation properties, but since the vinyl chloride copolymer itself has poor transparency, transparent formulations have the disadvantage of insufficient transparency, which limits the use of the copolymer. Further improvements were desired.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明の目的は、ゲル化特性と透明性に優れたポリ塩化
ビニルと高分子可塑剤の混練方法を提供することにある
An object of the present invention is to provide a method for kneading polyvinyl chloride and a polymer plasticizer that has excellent gelling properties and transparency.

〔問題点を解決するための手段〕[Means for solving problems]

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、透明性に優れた塩化ビニル系樹脂を
得るため鋭意研究した結果、ポリ塩化ビニルと高分子可
塑剤とを混練するに当り、高分子可塑剤を2回以上に分
割して混練することによりおどろくほどゲル化特性、透
明性が向上することを発見し本発明を完成した。
The inventors of the present invention have conducted intensive research to obtain a vinyl chloride resin with excellent gelling properties and transparency even with weak kneading machines such as two rolls and extruders. When kneading, the present invention was completed based on the discovery that by dividing the polymer plasticizer into two or more times and kneading, gelling properties and transparency were surprisingly improved.

すなわち、本発明は、ポリ塩化ビニルと高分子可塑剤と
を混練するに当り、高分子可塑剤の一部を添加して混練
し、次いで残りの高分子可塑剤を添加して混練すること
を特徴とするゲル化特性と透明性に優れたポリ塩化ビニ
ルと高分子可塑剤の混練方法である。
That is, in kneading polyvinyl chloride and a polymer plasticizer, the present invention includes adding a part of the polymer plasticizer and kneading, and then adding and kneading the remaining polymer plasticizer. This is a method of kneading polyvinyl chloride and a polymeric plasticizer, which are characterized by excellent gelling properties and transparency.

本発明では好ましくは1度目の混練でポリ塩化ビニル1
00重量部に対して高分子可塑剤5〜50重量部好まし
くは10〜40重量部を添加してペレット化を行ない、
2度目以上の混練時に残りの高分子可塑剤を添加し混練
する。
In the present invention, preferably in the first kneading, polyvinyl chloride 1
Pelletization is carried out by adding 5 to 50 parts by weight, preferably 10 to 40 parts by weight, of a polymer plasticizer to 00 parts by weight,
During the second or subsequent kneading, the remaining polymer plasticizer is added and kneaded.

1度目の高分子可塑剤の添加量がポリ塩化ビニル100
重量部に対して5重量部未満では高分子可塑剤が不足し
混練が十分性なわれにくいため練りムラが生じ易く、2
度目の混練を行なっても練りムラが残り、生産の品質の
バラツキとなるため好ましくない。又、高分子可塑剤の
添加量が50重量部以上では樹脂の溶融粘度が低くなり
すぎ、ポリ塩化ビニル中のプッが消えないために好まし
くない。
The first addition amount of polymer plasticizer is polyvinyl chloride 100
If it is less than 5 parts by weight, the polymer plasticizer will be insufficient and kneading will be difficult to achieve, resulting in uneven kneading.
Even after kneading for the second time, uneven kneading remains, which is undesirable because it causes variations in the quality of production. Further, if the amount of the polymer plasticizer added is 50 parts by weight or more, the melt viscosity of the resin becomes too low and the stickiness in the polyvinyl chloride is not eliminated, which is not preferable.

本発明の混練方法によって無可塑樹脂を得る方法は例え
ば、ヘンシェルミキサーにポリ塩化ビニル、安定剤、滑
剤、顔料、高分子可塑剤を投入しブレンドを行ないパウ
ダーを得る。このパウダーを押出機にてべt/ノットを
行ない、ヘンシェルミキサーを使用し残りの高分子可塑
剤とブレンドを行ない、再度押出機にてペレット化を行
なうことによりゲル化特性と透明性に優れた非移行性樹
脂が得られる。
To obtain a non-plastic resin by the kneading method of the present invention, for example, polyvinyl chloride, a stabilizer, a lubricant, a pigment, and a polymeric plasticizer are placed in a Henschel mixer and blended to obtain a powder. This powder is tied/knotted in an extruder, blended with the remaining polymer plasticizer using a Henschel mixer, and then pelletized in the extruder again, resulting in excellent gelling properties and transparency. A non-migrating resin is obtained.

必要に応じ充填剤、ゲル化促進剤、紫外線吸収剤、改質
剤等を添加しても良い。又、非移行性を損なわない範囲
で通常の可塑剤を添加しても何らさしつかえない。
If necessary, fillers, gelling promoters, ultraviolet absorbers, modifiers, etc. may be added. Further, there is no problem in adding a conventional plasticizer to the extent that the non-migration property is not impaired.

本発明に用いられるポリ塩化ビニルとしては、塩化ビニ
ルの単独重合体であり、例えば、ン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)ハルオキシジカーボネート
、ターシャリ−ブチルパーオキシビバレート等の有機過
酸化物;2,2’−アゾビスインブチロニトリル、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。
The polyvinyl chloride used in the present invention is a homopolymer of vinyl chloride, such as nrubitan higher fatty acid ester, polyoxyethylene sorbitan higher fatty acid ester, water-soluble cellulose derivative, polyvinyl alcohol, polyvinylpyrolidone, gelatin, etc. is used in combination as a dispersant, and as a catalyst, for example, benzoyl peroxide, lauroyl peroxide, caproyl peroxide, diisopropyl peroxydicarbonate, di(2-ethylhexyl) haloxydicarbonate, tert-butyl peroxybivalate, etc. organic peroxide; 2,2'-azobisinbutyronitrile; 2.
2'-azobis-2,4-dimethylvaleronitrile, 2
, 2'-azobis-4-methoxy-2,4-dimethylvaleronitrile and the like are preferably used alone or in combination to polymerize vinyl chloride.

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・−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、ブリード等の問
題から分子量10.000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・−酸化炭素の共重合体
からなる分子量10,000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。
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 oxide copolymers. Mention may be made of molecular plasticizers and modified products thereof. In addition, from the viewpoint of problems such as bleeding, a molecular weight of 10.000 or more is desirable. Among these, a polymeric plasticizer having a molecular weight of 10,000 or more and consisting of a copolymer of ethylene/vinyl acetate/carbon oxide is particularly effective in obtaining a polyvinyl chloride composition having oil resistance and extraction resistance.

本発明においては、高分子可塑剤の1部をまずポリ塩化
ビニルと混練しておき、次いで残りの高分子可塑剤と再
び混練することにより目的が達成されるのである。なお
、残りの高分子可塑剤は更に分割して混練してもかまわ
ない。
In the present invention, the object is achieved by first kneading a portion of the polymeric plasticizer with polyvinyl chloride and then kneading it again with the remaining polymeric plasticizer. Note that the remaining polymer plasticizer may be further divided and kneaded.

本発明を実施する場合、二本ロールや押出機等の練りの
弱い混練機を用いるわけであるが、生産性、作業性等を
考慮すると押出機を採用するのが好ましい。
When carrying out the present invention, a kneading machine with a weak kneading capacity, such as a two-roll machine or an extruder, is used, but in consideration of productivity, workability, etc., it is preferable to employ an extruder.

押出機としては、単軸、2軸、多軸、コニカルタイプを
単独又は2機以上を組み合わせて使用する。
As the extruder, single-screw, twin-screw, multi-screw, or conical types may be used alone or in combination of two or more.

本発明で混練した樹脂は、カレンダー、溶融押出し、ス
タンプインジェクション等の公知の方法により成型加工
されて実用に供される。
The resin kneaded in the present invention is molded by known methods such as calendering, melt extrusion, and stamp injection, and then put into practical use.

本発明にて混練した樹脂は、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、更に透明性に
優れているので医療用、産業用、食品用に好適に使用さ
れる。
The resin kneaded in the present invention has a smooth surface when molded because it has few ungelled particles, and has excellent transparency, so it is suitable for use in medical, industrial, and food applications. .

〔実施例〕〔Example〕

以下、実施例により本発明を説明する。 The present invention will be explained below with reference to Examples.

実施例−1 内容積501のヘンシェルミキサーにポリ塩化ビニル(
PVC) 15に9、安定剤、125に9、滑剤0.3
45に9を入れ高速で10分間攪拌ブレンドした。
Example-1 Polyvinyl chloride (
PVC) 15 to 9, stabilizer, 125 to 9, lubricant 0.3
9 was added to 45 and blended at high speed for 10 minutes.

その後、高分子可塑剤11エルバロイ74211(商標
)6kgを入れ攪拌ブレンドし、3分後に排出しpvc
/エルバロイ742ブレンド物を得た。
Then, 6 kg of polymer plasticizer 11 Elvaloy 74211 (trademark) was added and blended with stirring, and after 3 minutes, it was discharged and the PVC
/ Elvaloy 742 blend was obtained.

このブレンド物を2軸押用機池貝G T −110にて
、第1表の条件で混練しペレット化した。
This blend was kneaded and pelletized using a twin-screw extrusion machine Ikegai GT-110 under the conditions shown in Table 1.

このベレットに更に11エルバロイ742 ” 6 k
gを入れ、ヘンシェルミキサーにて3分間攪拌し、第1
表の2回目の条件で混練しペレット化した。
In addition to this beret 11 Elvaloy 742” 6k
g, stirred for 3 minutes with a Henschel mixer, and
The mixture was kneaded and pelletized under the second conditions shown in the table.

このペレットを180℃でプレスし、厚み0.5111
目 のシートを得、そのプツ、透明性を見視により調べたと
ころ、プッ、透明性は共に良好であった。
This pellet was pressed at 180℃ to a thickness of 0.5111
A transparent sheet was obtained, and its transparency was visually inspected, and it was found that both properties were good.

実施例−2 実施例−1で得たベレットに更に11エルバロイ742
 ” 6 k!9を入れヘンシェルミキサーに°C3分
間攪拌し、実施例−1の2回目の条件で混練し、ペレッ
ト化した。このペレットのプレスシートは、ブッ、透明
性共に良好であった。
Example-2 In addition to the pellet obtained in Example-1, 11 Elvaloy 742
6k!9 was placed in a Henschel mixer, stirred for 3 minutes at °C, and kneaded under the second conditions of Example 1 to form pellets. The pressed sheet of the pellets had good clarity and transparency.

実施例−3 実施例−1において、′1エルバロイ742 ”の使用
量を1回目3kg、2回目9kgに変更した以外は実施
例−1と同様に混練し、ペレット化した。
Example 3 Kneading and pelletization were carried out in the same manner as in Example 1, except that the amount of '1 Elvaloy 742'' used was changed to 3 kg in the first time and 9 kg in the second time.

このベレットのプレスシートは、プッ、透明性共に良好
であった。
The press sheet of this pellet was good in both visibility and transparency.

比較例−1 実施例−1において、嘗1エルバロイ742 ”の添加
量を一度にした以外は実施例−1と同様にしてブレンド
物を得、2軸押用機にて第1表の条件で混練し、ペレッ
ト化した。このペレットのプレスシートは、ブツが多く
、透明性も悪かった。
Comparative Example-1 A blend was obtained in the same manner as in Example-1, except that the amount of Elvaloy 742'' was added at once, and the mixture was processed using a twin-screw extruder under the conditions shown in Table 1. The mixture was kneaded and made into pellets.The pressed sheet of the pellets had many lumps and poor transparency.

〔発明の効果〕〔Effect of the invention〕

本発明では、上記構成をとるため、従来問題であった混
練不良によるブツの発生が防止されており、特に透明グ
レードの高分子可塑剤を用いた軟質塩化ビニル樹脂成形
品に有用である。
Since the present invention has the above-mentioned structure, the generation of lumps due to poor kneading, which has been a problem in the past, is prevented, and it is particularly useful for soft vinyl chloride resin molded products using transparent grade polymer plasticizers.

1日Hi顯j。I had a high face all day.

Claims (1)

【特許請求の範囲】[Claims] 1、ポリ塩化ビニルと高分子可塑剤とを混練するに当り
、高分子可塑剤の一部を添加して混練し、次いで残りの
高分子可塑剤を添加して混練することを特徴とするゲル
化特性と透明性に優れたポリ塩化ビニルと高分子可塑剤
の混練方法。
1. A gel characterized in that when kneading polyvinyl chloride and a polymer plasticizer, a part of the polymer plasticizer is added and kneaded, and then the remaining polymer plasticizer is added and kneaded. A method for kneading polyvinyl chloride and a polymer plasticizer with excellent chemical properties and transparency.
JP15919284A 1984-07-31 1984-07-31 Method of blending polyvinyl chloride with high polymer plasticizer Granted JPS6140326A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15919284A JPS6140326A (en) 1984-07-31 1984-07-31 Method of blending polyvinyl chloride with high polymer plasticizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15919284A JPS6140326A (en) 1984-07-31 1984-07-31 Method of blending polyvinyl chloride with high polymer plasticizer

Publications (2)

Publication Number Publication Date
JPS6140326A true JPS6140326A (en) 1986-02-26
JPH0522729B2 JPH0522729B2 (en) 1993-03-30

Family

ID=15688323

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15919284A Granted JPS6140326A (en) 1984-07-31 1984-07-31 Method of blending polyvinyl chloride with high polymer plasticizer

Country Status (1)

Country Link
JP (1) JPS6140326A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02129251A (en) * 1988-11-08 1990-05-17 Du Pont Mitsui Polychem Co Ltd Production of plasticized polyvinyl chloride mixture
JP2012149236A (en) * 2010-12-27 2012-08-09 Tokuyama Corp Method of producing vinyl chloride resin formed article
JP2017511758A (en) * 2014-02-13 2017-04-27 シーカ テクノロジー アクチェンゲゼルシャフト Method for producing plasticized PVC semi-finished product

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02129251A (en) * 1988-11-08 1990-05-17 Du Pont Mitsui Polychem Co Ltd Production of plasticized polyvinyl chloride mixture
JP2012149236A (en) * 2010-12-27 2012-08-09 Tokuyama Corp Method of producing vinyl chloride resin formed article
JP2017511758A (en) * 2014-02-13 2017-04-27 シーカ テクノロジー アクチェンゲゼルシャフト Method for producing plasticized PVC semi-finished product

Also Published As

Publication number Publication date
JPH0522729B2 (en) 1993-03-30

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