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JPS6034972B2 - Method for preventing plasticizer elution from soft vinyl chloride resin molded products - Google Patents
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JPS6034972B2 - Method for preventing plasticizer elution from soft vinyl chloride resin molded products - Google Patents

Method for preventing plasticizer elution from soft vinyl chloride resin molded products

Info

Publication number
JPS6034972B2
JPS6034972B2 JP13678379A JP13678379A JPS6034972B2 JP S6034972 B2 JPS6034972 B2 JP S6034972B2 JP 13678379 A JP13678379 A JP 13678379A JP 13678379 A JP13678379 A JP 13678379A JP S6034972 B2 JPS6034972 B2 JP S6034972B2
Authority
JP
Japan
Prior art keywords
vinyl chloride
temperature
chloride resin
resin molded
low
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
JP13678379A
Other languages
Japanese (ja)
Other versions
JPS5661433A (en
Inventor
潔 今田
進 上野
康秀 仁科
洋和 野村
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.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical 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 Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP13678379A priority Critical patent/JPS6034972B2/en
Priority to GB8033751A priority patent/GB2061968B/en
Priority to DE19803039853 priority patent/DE3039853A1/en
Priority to FR8022544A priority patent/FR2467864B1/en
Priority to NL8005813A priority patent/NL8005813A/en
Publication of JPS5661433A publication Critical patent/JPS5661433A/en
Publication of JPS6034972B2 publication Critical patent/JPS6034972B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/12Chemical modification
    • C08J7/123Treatment by wave energy or particle radiation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2327/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
    • C08J2327/02Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
    • C08J2327/04Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
    • C08J2327/06Homopolymers or copolymers of vinyl chloride

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

【発明の詳細な説明】 本発明は軟質塩化ビニル系樹脂成形品の可塑剤溶出防止
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preventing plasticizer elution from soft vinyl chloride resin molded articles.

欧質塩化ビニル系樹脂成形品については、このものが長
期間使用されている間に、可塑剤その他の添加剤が徐々
に成形品表面に移行しにじみ出るようになるという欠点
がある。
European vinyl chloride resin molded articles have the disadvantage that, while they are used for a long period of time, plasticizers and other additives gradually migrate to the surface of the molded article and ooze out.

この欠点を解決する方法として成形品表面を低温プラズ
マ処理する試みが行われており、これによれば成形品の
表面に架橋層が形成され、この架橋層による可塑剤溶出
(移行)防止効果が期待される。しかしながら、この低
温プラズマ処理はガス圧力、ガス流量、印加電力等の条
件を一定にしても再現性よく目的とする処理効果を得る
ことができず、こうした傾向はバッチ処理のみならず樹
脂成形品を連続的に低温プラズマ処理する場合にも認め
られ、その処理効果に信頼性がもてなかった。
As a way to solve this drawback, attempts have been made to treat the surface of the molded product with low-temperature plasma treatment. According to this method, a crosslinked layer is formed on the surface of the molded product, and this crosslinked layer has the effect of preventing plasticizer elution (migration). Be expected. However, this low-temperature plasma treatment cannot achieve the desired treatment effect with good reproducibility even if conditions such as gas pressure, gas flow rate, and applied power are kept constant. This was also observed when continuous low-temperature plasma treatment was performed, and the treatment effect was unreliable.

本発明者らはかかる技術的課題について鋭意研究した結
果、軟質塩化ビニル系樹脂成形品の低温プラズマ処理に
よる可塑剤溶出防止効果は、その被処理成形品の温度と
低温プラズマ発生のための入力側電極温度との関係に微
妙に影響されることを見出し、本発明に到達した。すな
わち、本発明は軟質塩化ビニル系樹脂成形品を内部電極
放電型低温プラズマ発生装置内に入れ、該成形品の温度
(T,。
As a result of intensive research into this technical problem, the present inventors found that the effect of preventing plasticizer elution by low-temperature plasma treatment of soft vinyl chloride resin molded products depends on the temperature of the molded product to be treated and the input side for low-temperature plasma generation. The present invention was achieved by discovering that this is subtly influenced by the relationship with the electrode temperature. That is, in the present invention, a soft vinyl chloride resin molded article is placed in an internal electrode discharge type low-temperature plasma generator, and the temperature of the molded article (T,.

0)および入力側電極温度(LOO)をそれぞれ、T,
=0〜800 す.−・o≦T2≦・oo−許. に保持しながら、10トル以下の無機ガスの低温プラズ
マで処理することを特徴とする軟質塩化ビニル系樹脂成
形品の可塑剤溶出防止方法に関するものであり、これに
よれば成形品表面に高密度架橋層を確実に形成すること
ができ、この架橋層による可塑剤溶出防止効果はきわめ
て顕著で、これが再現性よく達成されるという利点が与
えられる。
0) and the input side electrode temperature (LOO) are T,
=0~800 -・o≦T2≦・oo-allow. The present invention relates to a method for preventing plasticizer elution from soft vinyl chloride resin molded products, which is characterized by treating with low-temperature plasma of an inorganic gas of 10 torr or less while maintaining the temperature of the molded product. The advantage is that a crosslinked layer can be reliably formed, the effect of preventing plasticizer elution by this crosslinked layer is extremely remarkable, and this can be achieved with good reproducibility.

以下本発明の方法を詳細に説明する。まず、本発明の方
法が実施される軟質塩化ビニル系樹脂成形品は、樹脂原
料としてポリ塩化ビニルを主体とする英重合体を用いて
成形した成形品であればフィルムないしシート状体、チ
ューブ、ホース等の管状体、その他異形成形体のいずれ
も対象とされ、成形品の形状、種類等に制限はない。
The method of the present invention will be explained in detail below. First, the soft vinyl chloride resin molded product to which the method of the present invention is carried out is a film or sheet-like product, a tube, This applies to both tubular bodies such as hoses and other irregularly shaped bodies, and there are no restrictions on the shape or type of molded articles.

上記塩化ビニルを主体とする共重合体としては、塩化ビ
ニルー酢酸ビニル共重合体、塩化ビニルーェチレン共重
合体、塩化ビニループロピレン共重合体、塩化ビニルー
ェチレンー酢酸ビニル共重合体、塩化ビニルーアクリロ
ニトリル共重合体、塩化ビニルースチレン共重合体、塩
化ビニルースチレンープタジェン共重合体、塩化ビニル
ー塩化ビニリデン共重合体、さらにはポリ塩化ビニルを
主体とするグラフト共重合体が例示される。
Examples of copolymers mainly composed of vinyl chloride include vinyl chloride-vinyl acetate copolymer, vinyl chloride-ethylene copolymer, vinyl chloride-propylene copolymer, vinyl chloride-ethylene vinyl acetate copolymer, and vinyl chloride-vinyl acetate copolymer. Examples include acrylonitrile copolymer, vinyl-styrene chloride copolymer, vinyl-styrene chloride-ptadiene copolymer, vinyl chloride-vinylidene chloride copolymer, and graft copolymers mainly composed of polyvinyl chloride.

これらの塩化ビニル系樹脂は1種類に限られず、2種以
上のブレンドとして使用してもよく、また成形品の機械
的強度等を改良する目的で他の合成樹脂が配合されても
よく、この合成樹脂としてはエチレン−酢酸ビニル共重
合体、アクリロニトリルーブタジェン共重合体、スチレ
ンーアクリロニトリル共重合体、メチルメタクリレート
ースチレンーブタジェン共重合体、アクリロニトリルー
スチレンーブタジェン共重合体、エチレンープロピレン
エラストマー、エチレンープロピレン−ジェンェラスト
マー、ポリアミド樹脂、カプロラクタム重合体、ェポキ
シ変性ポリブタジェン、ェポキシ変性ポリオール、オル
ガノポリシロキサン等が例示される。軟質塩化ビニル系
樹脂成形品を得るために可塑剤が使用されるが、この可
塑剤としてはフタル酸ジェチル、フタル酸ジー2ーェチ
ルヘキシル、フタル酸ジノニル等のフタル酸ェステル、
トリメリット酸トリメチル、トリメリット酸トリオクチ
ル等のトリメリツト酸ェステル、アジピン酸ジオクチル
、アジピン酸ジィソデシル、アゼラィン酸ジオクチル等
の脂肪族二塩基酸ェステル、オレイン酸ブチル、アセチ
ルリシノール酸メチル、塩素化脂肪酸メチル等の脂肪酸
ェステル、エチルフタリルエチレングリコレート、ジエ
チレングリコールジベンゾェート、アセチルクェン酸ト
リブチル等の可塑剤が例示される。
These vinyl chloride resins are not limited to one type, but may be used as a blend of two or more types, and other synthetic resins may be blended for the purpose of improving the mechanical strength etc. of the molded product. Examples of synthetic resins include ethylene-vinyl acetate copolymer, acrylonitrile-butadiene copolymer, styrene-acrylonitrile copolymer, methyl methacrylate-styrene-butadiene copolymer, acrylonitrile-styrene-butadiene copolymer, and ethylene-vinyl acetate copolymer. Examples include propylene elastomer, ethylene-propylene-lene elastomer, polyamide resin, caprolactam polymer, epoxy-modified polybutadiene, epoxy-modified polyol, and organopolysiloxane. Plasticizers are used to obtain soft vinyl chloride resin molded products, and these plasticizers include phthalate esters such as diethyl phthalate, di-2-ethylhexyl phthalate, and dinonyl phthalate;
Trimellitic acid esters such as trimethyl trimellitate and trioctyl trimellitate, aliphatic dibasic acid esters such as dioctyl adipate, disodecyl adipate, and dioctyl azelate, butyl oleate, methyl acetyl ricinoleate, chlorinated fatty acid methyl, etc. Examples of plasticizers include fatty acid esters, ethyl phthalyl ethylene glycolate, diethylene glycol dibenzoate, and tributyl acetyl citrate.

このほか必要に応じ使用される各種添加剤たとえば安定
剤、滑剤、充てん剤、顔料、染料、紫外線吸収剤、抗酸
化剤、架橋剤、加硫促進剤、各種界面活性剤(カチオン
、アニオン、ノニオン、両性)が適宜に配合されること
は差支えない。
In addition, various additives are used as necessary, such as stabilizers, lubricants, fillers, pigments, dyes, ultraviolet absorbers, antioxidants, crosslinking agents, vulcanization accelerators, and various surfactants (cationic, anionic, nonionic). , amphoteric) may be appropriately blended.

軟質塩化ビニル系樹脂成形品を得る手段としては、押出
成形、射出成形、カレンダー成形、インフレーション成
形、圧縮成形等従来塩化ビニル系樹脂の成形で採用され
ている成形方法によればよい。こうして得られる成形品
は低温プラズマ処理されるのであるが、本発明の方法に
おいてはプラズマ発生装置として内部電極放電型低温プ
ラズマ発生装置を使用し、かつプラズマ処理条件を被処
理成形品の温度をT,℃とし、入力側電極温度をT2℃
とした場合に、T,=0〜80 浄′・雌2≦loo−計. を満足することが必要とされる。
The soft vinyl chloride resin molded article may be obtained by any conventional molding method for vinyl chloride resins, such as extrusion molding, injection molding, calendar molding, inflation molding, or compression molding. The molded product thus obtained is subjected to low-temperature plasma treatment, and in the method of the present invention, an internal electrode discharge type low-temperature plasma generator is used as the plasma generator, and the plasma treatment conditions are set such that the temperature of the molded product to be treated is T. , ℃, and the input side electrode temperature is T2℃.
In this case, T, = 0 to 80 pure'・female 2≦loo-total. is required to satisfy.

この条件を満足しない場合には可塑剤熔出防止効果を再
現性よく安定して達成することが困難となる。内部電極
放電型の低温プラズマ発生装置は、電極が発生装置内部
に無機ガスと接して置かれた形式のものであり、内部に
導入された低圧無機ガスは電極付近でプラズマ化され、
これが発生装置内に置かれた成形品の表面に作用し、目
的の処理すなわち成形品表面における高密度架橋層の形
成が達成される。
If this condition is not satisfied, it will be difficult to stably achieve the effect of preventing plasticizer melting with good reproducibility. An internal electrode discharge type low temperature plasma generator is a type in which an electrode is placed inside the generator in contact with an inorganic gas, and the low pressure inorganic gas introduced inside is turned into plasma near the electrode.
This acts on the surface of the molded article placed in the generator and achieves the desired treatment, namely the formation of a dense crosslinked layer on the surface of the molded article.

入力側電極としては平板型、ネット型、コイル状型、榛
型等各種形状のものが選択使用されるが、本発明におい
ては前記した温度条件を満足するための温度制御手段が
設けられていることが必要であり、このためには電極内
部に熱媒体を流すことができる形式の電極を使用するこ
とが望ましい。
The input side electrode can be selected from various shapes such as a flat plate type, a net type, a coil type, and a comb type, but in the present invention, a temperature control means is provided to satisfy the above-mentioned temperature conditions. For this purpose, it is desirable to use an electrode that allows a heating medium to flow inside the electrode.

なお、電極は直接低温プラズマガスにさらされるため、
化学的に安定な材料を用いるかまたはガラス、ホウロウ
等で被覆されていることが望ましい。彼処理成形品の温
度制御はたとえば接地側電極として温度制御可能な金属
製平板状電極を使用し、この電極上に該彼処理成形品を
鼓層して電極温度制御によりその戦暦された成形品温度
を制御するという方法等によればよい。
In addition, since the electrode is directly exposed to low-temperature plasma gas,
It is desirable to use a chemically stable material or to coat it with glass, enamel, or the like. To control the temperature of a processed molded product, for example, a temperature-controllable metal flat plate electrode is used as the ground side electrode, and the processed molded product is placed on top of this electrode, and the temperature of the processed molded product is controlled by the electrode temperature control. A method such as controlling the temperature of the product may be used.

またチューブ状の成形体を連続的に低温プラズマ処理す
る場合であればチューブ内に所定温度の熱媒体を流す手
段が便利である。低温プラズマの発生は、装置内に無機
ガスを導入し、たとえば電極に13.58の比、10〜
700Wの電力を印加すればよい。
Further, when a tube-shaped molded body is subjected to continuous low-temperature plasma treatment, it is convenient to flow a heat medium at a predetermined temperature into the tube. Generation of low-temperature plasma can be achieved by introducing an inorganic gas into the device, and applying a ratio of 13.58 to the electrodes, for example, 10 to 10.
A power of 700W may be applied.

成形品の低温プラズマ処理時間は印加電圧によっても相
違するが、一般には数秒から数十分とすることで十分で
ある。低温プラズマ発生のための放電周波数帯としては
上記した高周波のほかに、低周波、マイクロ波、直流な
どを用いることができる。無機ガスとしてはヘリウム、
ネオン、アルゴン、窒素、亜鉛化窒素、二酸化窒素、酸
素、空気、一酸化炭素、二酸化炭素、水素、塩素、さら
には塩化水素、亜硫酸ガス、硫化水素などが例示され、
これらのガスは単独または混合して使用される。
Although the low-temperature plasma treatment time for a molded article varies depending on the applied voltage, generally a few seconds to several tens of minutes is sufficient. As the discharge frequency band for generating low-temperature plasma, in addition to the above-mentioned high frequency, low frequency, microwave, direct current, etc. can be used. Helium is an inorganic gas,
Examples include neon, argon, nitrogen, zincated nitrogen, nitrogen dioxide, oxygen, air, carbon monoxide, carbon dioxide, hydrogen, chlorine, as well as hydrogen chloride, sulfur dioxide gas, and hydrogen sulfide.
These gases may be used alone or in combination.

これらガスのプラズマ発生装置内におけるガス圧力は目
的の低温プラズマが容易に発生するような圧力すなわち
10トル以下(好ましくは0.01トル〜1トル)とす
ることが必要とされる。このようにして成形品を低温プ
ラズマ処理することにより、極短時間で成形品の表面に
目的とする高密度架橋層が生成し、これにより可塑剤等
の添加剤が成形品の表面ににじみ出る現象が完全に抑制
され、かつまた形成された表面架橋層(バリアー層)は
柔軟性に富むという注目すべき成形品が得られる。・つ
ぎに、本発明の実施例をあげる。
The gas pressure of these gases in the plasma generator is required to be such that the desired low-temperature plasma can be easily generated, that is, 10 Torr or less (preferably 0.01 Torr to 1 Torr). By subjecting the molded product to low-temperature plasma treatment in this way, the desired high-density crosslinked layer is generated on the surface of the molded product in an extremely short time, and this causes additives such as plasticizers to ooze out onto the surface of the molded product. A remarkable molded article is obtained in which the formation of a surface crosslinked layer (barrier layer) is completely suppressed, and the formed surface crosslinked layer (barrier layer) is highly flexible. - Next, examples of the present invention will be given.

実施例 1 塩化ビニル樹脂(TK−1300、信越化学社製商品名
)10の重量部、DOP5の重量部、ステアリン酸カル
シウム1.5重量部、ステアリン酸亜鉛1.5重量部よ
りなる配合物を16000で10分間ロール泥練し、こ
れを16500でプレス成形して厚さ0.5側のシート
に作成した。
Example 1 16,000 parts by weight of a blend consisting of 10 parts by weight of vinyl chloride resin (TK-1300, trade name manufactured by Shin-Etsu Chemical Co., Ltd.), parts by weight of DOP5, 1.5 parts by weight of calcium stearate, and 1.5 parts by weight of zinc stearate. The mixture was kneaded with a roll for 10 minutes, and then press-molded at 16500 to form a sheet with a thickness of 0.5.

このシートの1片(試料シート)を内部電極放電型低温
プラズマ発生装置内の金属平板状の接地側電極上に置き
、装置内に一酸化炭素ガスを通気しながら圧力を1.0
トルに調整保持し、装置内の入力側電極および該接地側
電極の両方をそれら内部に熱媒体を循環させることによ
り温度制御し、試料シートは接地側電極と同じ温度に保
たれるようにした。
One piece of this sheet (sample sheet) was placed on the flat metal ground electrode in an internal electrode discharge type low-temperature plasma generator, and the pressure was increased to 1.0 while carbon monoxide gas was passed through the device.
The temperature of both the input side electrode and the ground side electrode in the device was controlled by circulating a heating medium inside them, so that the sample sheet was kept at the same temperature as the ground side electrode. .

入力側電極に13.58MHZ、 500Wの高周波を
印加することにより低温プラズマを発生させ、試料シー
トを1分間低温プラズマ処理した。上記において入力側
電極および試料シートの温度を種々の値に制御して行っ
たそれぞれの処理シートについて、下記に示す試験法で
nーヘキサン抽出した際の可塑剤(DOP)抽出量を調
べたところ、第1表に示すとおりの結果が得られた。n
−へキサン抽出量測定法:100の【の円筒形抽出容器
の底にシートをセットし、この2金あの表面と50机【
のn−へキサンとを接触させ、370のウオーターバス
中で2時間振とうして、nーヘキサン中に抽出された可
塑剤(DOP)の量をガスクロマトグラフイにより定量
分析した。
Low-temperature plasma was generated by applying a high frequency of 13.58 MHZ and 500 W to the input side electrode, and the sample sheet was subjected to low-temperature plasma treatment for 1 minute. The amount of plasticizer (DOP) extracted during n-hexane extraction was investigated using the test method shown below for each of the treated sheets in which the temperatures of the input side electrode and sample sheet were controlled to various values in the above process. The results shown in Table 1 were obtained. n
- Hexane extraction amount measurement method: Set a sheet at the bottom of a cylindrical extraction container of 100 [
of n-hexane and shaken for 2 hours in a 370 water bath, and the amount of plasticizer (DOP) extracted into the n-hexane was quantitatively analyzed by gas chromatography.

第1表 可塑剤抽出量(唆し26が) 施例 2 前例と同様にして作成した試料シートを2の女用意した
Table 1 Amount of plasticizer extracted (indication 26) Example 2 A sample sheet prepared in the same manner as in the previous example was prepared.

そのうち1の女の各々については、入力側電極温度:4
0q0に制御試料温度:40ooに制御 COガスの圧力:0.5トル 高周波:13.58M比、300W 処理時間:2分 としたほかは前例と同様にして低温プラズマ処理し、可
塑剤抽出量を測定した。
For each of the 1 women, the input side electrode temperature: 4
Controlled sample temperature at 0q0: Controlled at 40oo CO gas pressure: 0.5 Torr High frequency: 13.58M ratio, 300W Treatment time: Low temperature plasma treatment was performed in the same manner as in the previous example except that it was 2 minutes to reduce the amount of plasticizer extracted. It was measured.

他の試料シート1の女の各々については、入力側電極お
よび試料の温度コントロールを全く行わなかったほかは
上記と同様にして低温プラズマ処理し、可塑剤抽出量を
測定した。
For each of the other female sample sheets 1, the low-temperature plasma treatment was performed in the same manner as above, except that the temperature of the input electrode and the sample was not controlled at all, and the amount of plasticizer extracted was measured.

上託したそれぞれの結果は第2表に示すとおりであり、
これらの結果から入力側電極および試料の温度コントロ
ールをすることにより、十分な処理効果を再現性よく達
成することができるが、該温度コントロールを行わない
と処理効果が大中にバラッキ、再現性がきわめて悪いこ
とが判る。
The results of each submission are shown in Table 2.
From these results, it is possible to achieve sufficient processing effects with good reproducibility by controlling the temperature of the input side electrode and sample, but if temperature control is not performed, the processing effects will vary widely and reproducibility will be poor. It turns out to be extremely bad.

第2表(鹿第1隻隊蝉、)Table 2 (Deer 1st Fleet Cicada)

Claims (1)

【特許請求の範囲】 1 軟質塩化ビニル系樹脂成形品を内部電極放電型低温
プラズマ発生装置内に入れ、該成型品の温度(T_1℃
)および入力側電極温度(T_2℃)をそれぞれ、T_
1=0〜80 3/8T_1−10≦T_2≦100−5/8T_1に
保持しながら、10トル以下の無機ガスの低温プラズマ
で処理することを特徴とする軟質塩化ビニル系樹脂成形
品の可塑剤溶出防止方法。
[Claims] 1. A soft vinyl chloride resin molded product is placed in an internal electrode discharge type low temperature plasma generator, and the temperature of the molded product (T_1°C
) and input side electrode temperature (T_2℃), respectively.
1=0~80 3/8T_1-10≦T_2≦100-5/8Plasticizer for soft vinyl chloride resin molded products, characterized by being treated with low-temperature plasma of inorganic gas of 10 torr or less while maintaining 10≦T_2≦100-5/8T_1 How to prevent elution.
JP13678379A 1979-10-23 1979-10-23 Method for preventing plasticizer elution from soft vinyl chloride resin molded products Expired JPS6034972B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP13678379A JPS6034972B2 (en) 1979-10-23 1979-10-23 Method for preventing plasticizer elution from soft vinyl chloride resin molded products
GB8033751A GB2061968B (en) 1979-10-23 1980-10-20 Method for preventing bleeding of plasticizers on the surface of a shaped article of plasticized polyvinyl chloride resin
DE19803039853 DE3039853A1 (en) 1979-10-23 1980-10-22 METHOD FOR SUPPRESSING SOFTENER EXHAUST ON MOLDING SURFACES OF POLYVINYL CHLORIDE RESINS CONTAINING SOFTENERS
FR8022544A FR2467864B1 (en) 1979-10-23 1980-10-22 PROCESS FOR PREVENTING EXUDATION OF PLASTICIZERS ON THE SURFACE OF ARTICLES MADE OF PLASTICIZED POLYVINYL CHLORIDE RESINS
NL8005813A NL8005813A (en) 1979-10-23 1980-10-22 METHOD FOR PREVENTING THE SCREAMING OF WEATHER MAKERS ON THE SURFACE OF A FORMED ARTICLE OF PLASTICATED POLYVINYL CHLORIDE RESIN

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13678379A JPS6034972B2 (en) 1979-10-23 1979-10-23 Method for preventing plasticizer elution from soft vinyl chloride resin molded products

Publications (2)

Publication Number Publication Date
JPS5661433A JPS5661433A (en) 1981-05-26
JPS6034972B2 true JPS6034972B2 (en) 1985-08-12

Family

ID=15183407

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13678379A Expired JPS6034972B2 (en) 1979-10-23 1979-10-23 Method for preventing plasticizer elution from soft vinyl chloride resin molded products

Country Status (5)

Country Link
JP (1) JPS6034972B2 (en)
DE (1) DE3039853A1 (en)
FR (1) FR2467864B1 (en)
GB (1) GB2061968B (en)
NL (1) NL8005813A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53114875A (en) * 1977-03-18 1978-10-06 Agency Of Ind Science & Technol Method for preventing elusion of plasticizer from polyvinyl chloride medical material

Also Published As

Publication number Publication date
FR2467864B1 (en) 1985-11-22
FR2467864A1 (en) 1981-04-30
JPS5661433A (en) 1981-05-26
GB2061968A (en) 1981-05-20
NL8005813A (en) 1981-04-27
GB2061968B (en) 1983-05-18
DE3039853A1 (en) 1981-05-14

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