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JPH056502B2 - - Google Patents
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JPH056502B2 - - Google Patents

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Publication number
JPH056502B2
JPH056502B2 JP60053020A JP5302085A JPH056502B2 JP H056502 B2 JPH056502 B2 JP H056502B2 JP 60053020 A JP60053020 A JP 60053020A JP 5302085 A JP5302085 A JP 5302085A JP H056502 B2 JPH056502 B2 JP H056502B2
Authority
JP
Japan
Prior art keywords
vinyl chloride
compression set
molded product
chloride resin
heat treatment
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 - Fee Related
Application number
JP60053020A
Other languages
Japanese (ja)
Other versions
JPS61211021A (en
Inventor
Tatsuo Hasue
Kazumasa Yamane
Teizo Saito
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 JP60053020A priority Critical patent/JPS61211021A/en
Publication of JPS61211021A publication Critical patent/JPS61211021A/en
Publication of JPH056502B2 publication Critical patent/JPH056502B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C71/00After-treatment of articles without altering their shape; Apparatus therefor
    • B29C71/02Thermal after-treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C71/00After-treatment of articles without altering their shape; Apparatus therefor
    • B29C71/02Thermal after-treatment
    • B29C2071/022Annealing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2027/00Use of polyvinylhalogenides or derivatives thereof as moulding material
    • B29K2027/06PVC, i.e. polyvinylchloride

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Description

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

[産業上の利用分野] 本発明は塩化ビニル系樹脂組成物を射出成形や
押出成形法により成形加工してえられた成形品を
加熱処理することにより、圧縮永久歪や永久伸び
などの永久歪を小さくした車輌用の成形品を製造
する方法に関する。さらに詳しくは、パツキン
類、チユーブ、ガスケツト、グラスランチヤンネ
ル、ウエザーストリツプなどのように高弾性が必
要とされる車輌用に利用される永久歪を小さくし
た軟質塩化ビニル系成形品を製造する方法に関す
る。 [従来の技術] 一般に塩化ビニル系樹脂に可塑剤を添加すると
適度の弾力性を有する柔軟性に富んだ成形品がえ
られ、種々の分野に利用されている。 [発明が解決しようとする問題点] しかしながら、一般の軟質塩化ビニル系樹脂組
成物から成形加工によりつくられる成形品は圧縮
永久歪が大きく、応力を加えたのちの復元力が劣
るという欠点を有しており、パツキン、グロメツ
トなどの射出成形品や、押出成形によりえられる
ウエザーストリツプ、ドアガラスストリツプ、ド
アグラスランなどの自動車品、ガスケツト類など
のように小さな圧縮永久歪が要求される用途への
使用が制限されている。 この技術課題を解決する手段として、平均重合
度の高い塩化ビニル系樹脂を用いる方法、特開昭
54−80354号公報、特開昭56−79141号公報などに
開示されているように、テトラヒドロフランに不
溶なゲル分を有する部分的に架橋させた塩化ビニ
ル系樹脂を用いる方法、あるいは特開昭56−
115342号公報、特開昭59−51933号公報などに開
示されているように、メチルエチルケトンに不溶
なゲル分を有する部分的に架橋したアクリロニト
リル−ブタジエン系共重合体を塩化ビニル系樹脂
にブレンドした組成物を用いる方法などにより、
圧縮永久歪はある程度改良しうることは一般に知
られているが、イオウや有機過酸化物で加硫した
EPDM、NBR、クロロプレンゴムなどと比べる
圧縮永久歪は大きく、用途は限定されているのが
実情である。 本発明は一般の軟質塩化ビニル系樹脂組成物を
射出成形してえられたパツキング、グロメツトな
どの成形品、押出成形してえられたウエザースト
リツプ、ドアグラスランなどの自動車部品やガス
ケツトなどの成形品の圧縮永久歪が大きく、用途
が制限されているという問題や、高重合度の塩化
ビニル系樹脂あるいはテトラヒドロフランに不溶
なゲル分を有する部分架橋塩化ビニル系樹脂の使
用、またはこれらの塩化ビニル系樹脂にメチルエ
チルケトンに不溶なゲル分を有する部分架橋アク
リロニトリル−ブタジエン系共重合体をブレンド
した軟質塩化ビニル系樹脂組成の使用などによ
り、えられる成形品の圧縮永久歪は通常の塩化ビ
ニル系樹脂組成物からえられる成形品と比べると
改良されるものの、イオウや有機過酸化物で加硫
したEPDM、NBR、クロロプレンゴムと比べる
と、圧縮永久歪などの物性が劣り、用途が制限さ
れているという問題などを解決するためになされ
たものである。 [問題点を解決するための手段] 本発明は、塩化ビニル系樹脂100部(重量部、
以下同様)および可塑剤20〜200部よりなる塩化
ビニル系樹脂組成物を成形加工してえられた成形
品を50〜120℃の温度20分〜24時間加熱処理する
ことを特徴とする車輌用の射出成形品または押出
成形品を製造する方法に関する。 [実施例] 本発明に用いる塩化ビニル系樹脂とは、塩化ビ
ニルモノマーを単独重合させた塩化ビニル系樹
脂、または塩化ビニルを主成分とする、すなわち
85%(重量%、以下同様)以上含有する塩化ビニ
ル共重合樹脂であり、後者の具体例としては、た
とえば塩化ビニル−酢酸ビニル共重合樹脂、塩化
ビニル−エチレン共重合樹脂、塩化ビニル−プロ
ピレン共重合樹脂、塩化ビニルとアクリル酸また
はそのエステルとの共重合樹脂、塩化ビニルとメ
タクリル酸またはそのエステルとの共重合樹脂、
塩化ビニルとアルキルビニルエーテルとの共重合
樹脂などがあげられるが、これらに限定されるも
のではない。これらの塩化ビニル共重合樹脂は塩
化ビニル樹脂に対して劣位量(30%まで)ブレン
ドして使用してもよい。 本発明に用いる塩化ビニル系樹脂としては、さ
ら前記塩化ビニル系樹脂以外の特開昭56−81325
号公報、特開昭56−81328号公報、特開昭57−
195711号公報などに開示されているテトラヒドロ
フランに不溶なゲル分を有する、部分的に架橋さ
れた塩化ビニル系樹脂を用いてもよい。 本発明に用いる可塑剤は本発明に用いる樹脂組
成物を軟質化するために加えられるものであり、
その添加量は塩化ビニル系樹脂に対して20〜200
部、好ましくは30〜160部である。前記添加量が
20部未満になると成形品が充分柔軟化されず、熱
処理による永久歪を小さくするという効果、すな
わちゴム的性質の発現が生じない。 一方、該量が200部をこえるとドライアツプし
難くなり、射出成形後や押出成形後の成形品がべ
とつくなど、加工面や実用上の問題があり好まし
くない。 前記可塑剤としては、たとえばジオクチルフタ
レート、ジノニルフタレート、ジイソデシルフタ
レートなどのフタル酸系可塑剤、アジピン酸ジオ
クチル、アゼライン酸ジオクチルなどの脂肪酸系
可塑剤、トリメリツト酸トリオクチルなどのトリ
メリツト酸系可塑剤、ポリエステル系可塑剤、エ
ポキシ化大豆油などのエポキシ化物、トリクレジ
ルホスフエートなどのリン酸系可塑剤、塩素化パ
ラフインなど、通常軟質塩化ビニル系樹脂組成物
に用いられる可塑剤があげられ、単独で用いても
よく、2種以上併用してもよく、とくに限定なく
使用することができる。 本発明においては塩化ビニル系樹脂および可塑
剤から塩化ビニル系樹脂組成物が調製されるが、
ゴム物質を加えてもよい。 このようなゴム物質としては、たとえばアクリ
ロニトリル−ブタジエン共重合体、エチレン−酢
酸ビニル共重合体、エチレン−酢酸ビニル−一酸
化炭素3元共重合体、塩素化ポリエチレン、熱可
塑性ポリウレタン、熱可塑性ポリエステル、クロ
ロプレンゴム、アクリルゴムなどがあげられる。
これらのゴム物質のなかでは、特開昭59−51933
号公報に開示されているように、メチルエチルケ
トンに対する溶解性が90%以下であり、その製造
時にジビニルベンゼンなどの多官能性モノマーを
その重合系に加えて重合し、分子中に架橋構造を
もたせたアクリロニトリル−ブタジエン共重合体
が圧縮永久歪を小さくする効果があり、とくに好
ましい。 前記ゴム物質は単独で用いてもよく、2種以上
併用してもよく、その使用量としては塩化ビニル
系樹脂100部に対して150部以下の範囲で使用する
のがよい。該量が150部をこえると、加工性がわ
るくなつたり、塩化ビニル系樹脂が有する耐熱老
化性、耐オゾン性、機械的物性などが良好である
などの固有の特性が失なわれる傾向が生ずるなど
するため好ましくない。 さらに必要に応じて熱安定剤、充填剤、滑剤、
紫外線吸収剤、顔料、アゾジカルボンアミドなど
の発泡剤、メチルメタクリレートとアクリル酸ブ
チルとの共重合体などの加工助剤などを配合して
使用してもよい。必要に応じて使用される副成分
の種類および量は目的に応じて前記割合を満足す
る範囲で適宜選択して用いればよい。 本発明に用いる樹脂組成物は、従来の軟質塩化
ビニル系樹脂組成物と同様の工程で混合、混練し
て造粒され、射出成形や押出成形などの方法で成
形加工されうる。 すなわち、スーパーミキサー、リボンブレンダ
ーなどの混合機を用いて、必要により安定剤など
とともに混合することができ、これらの混合物は
バンバリーミキサー、ミキシングロール、押出機
などにより混練され造粒される。造粒されたペレ
ツトはプレス成形、射出成形、押出成形などの方
法で成形され、えられた成形品を50〜120℃、好
ましくは50〜110℃の温度で20分間以上、好まし
くは1時間以上加熱処理することにより成形品の
永久歪、とりわけ圧縮永久歪が大幅に減少する。 成形品の加熱処理は熱風乾燥機などの加熱炉中
に静置するだけでよい。前記加熱処理温度が50℃
未満では永久歪、とくに圧縮永久歪は改良され
ず、120℃をこえると成形品が変型して形状を保
持できなくなつたりするので好ましくない。また
加熱処理時間が20分間未満になると、圧縮永久歪
を小さくすることができなくなる。 以下本発明の方法を実施例にもとづき説明する
が、本発明はこれらに限定されるものではない。 なお実施例中の各物性置はつぎの方法により測
定した。 (テトラヒドロフランに不溶なゲル分) ソツクスレ−抽出器を用いて熱テトラヒドロフ
ランで22時間抽出し、350メツシユのフイルター
で分離された抽出残渣を測定。 (NBRのメチルエチルケトン(以下、MEKとい
う)に対する溶解性) ブロツク状NBR1gをMEK100ml中に25℃で48
時間浸漬し、溶液および粒子として100メツシユ
のフイルターを通過したものの割合を測定。 (成形品の圧縮永久歪) 圧縮永久歪測定用試験片は次の3種類の加工法
により作製し、成形品の圧縮永久歪を測定。 (1) プレス成形品の作り方と測定法 第1表に示す各配合系のドライブレンド物を
ロール温度160℃(配合2、3のものは175℃)
で7分間混練し、厚さ約3mmの素練りのシート
を作製し、えられたシートを重ね合わせて170
℃(配合2、3のものは180℃)で4分間余熱
したのち、170℃(配合2、3のものは180℃)
で3分間、150Kg/cm2の荷重をかけて厚さ12.7
mmのプレス板をつくり、直径29.0mmの直円柱状
にくり抜き、第2表の条件で熱処理し、JIS K
6301に準拠し、圧縮率25%、圧縮条件70℃で
22時間後の圧縮永久歪を測定。 (2) 射出成形品の作り方と測定法 第1表に示す各配合系を前記と同じ方法、条
件にて厚さ約3mmの素練のシートを作製し、え
られたシートを約3mm四方に切断してペレツト
とし、そのペレツトを用いて型締圧150トン、
射出容量173cm3/シヨツトの射出成形機にて、
厚さ12mm、縦50mm、横100mmの金型を用いてシ
リンダー温度165℃(配合3のものは180℃)、
ノズル温度160℃(配合3のものは、175℃)、
射出圧力50Kg/cm2で射出成形した。 えられた成形板から直径29.0mmの直円柱状物
をくり抜き、第3表の条件で熱処理してJIS K
6301準拠し、圧縮率25%、圧縮条件70℃で22
時間後の圧縮永久歪を測定。 (3) 押出成形品の作り方と測定法 第1表に示す配合3のものを前記と同方法、
条件にて厚さ約3mmの素練りシートを作製し、
えられたシートを約3mm四方に切断してペレツ
トとし、そのペレツトを用いてL/D=22で圧
縮比3.0のフルフライトスクリユーを使用した
50mm単軸押出機にて第1図に示した異形押出成
形品(自動車用シール部材)(1)を押出し、第4
表の条件で熱処理し、その成形品を第2図に示
すスペーサー3を有する装置2を用いてJIS K
6301の圧縮永久歪測定法と同じ方法で測定し
た。なお圧縮率は53%、圧縮条件は70℃で22時
間であり、押出成形条件はホツパー側よりシリ
ンダー温度C1 150℃、C2 160℃、C3 170℃、
C4 175℃、ダイ温度175℃に設定し、スクリユ
ー回転数は30rpmであつた。 (熱処理後の外観) 前記のプレス成形、射出成形および押出成形し
た各成形品を熱風乾燥機中に静置し、第2表、第
3表、第4表の熱処理条件にて熱処理し、外観の
艶の変化を観察し、下記基準にもとづき評価し
た。 ○:変化なし △:変化小 ×:変化大 実施例1〜6および比較例1〜2 第1表に示す配合物をロール混練し、えられた
素練りシートからプレス成形品を作製し、該成形
品を第2表の熱処理条件の熱風乾燥機のなかに静
置し、熱処理後の外観を観察するとともに、JIS
K 6301に準拠して圧縮永久歪を測定した。結果
を第2表に示す。 なお第1表中のS 1003およびS3000はそれぞ
れ鐘淵化学工業(株)製のカネビニールS1003(=
1300)およびカネビニールS3000(3200)、部分
架橋塩化ビニル樹脂はTHF不溶分19%の部分架
橋塩化ビニル樹脂、アクリニトリル−ブタジエン
共重合体はアクリニトリル分含量33%、MEK溶
解性21%、ムーニー粘度50のアクリニトリル−ブ
タジエン共重合体、DOPはジオクチルフタレー
トである。
[Industrial Application Field] The present invention heat-treats a molded product obtained by molding a vinyl chloride resin composition by injection molding or extrusion, thereby reducing permanent deformation such as compression set and permanent elongation. The present invention relates to a method of manufacturing a molded product for a vehicle that is smaller in size. More specifically, the method for manufacturing soft vinyl chloride molded products with low permanent deformation that are used for vehicles that require high elasticity, such as gaskets, tubes, gaskets, glass launch channels, weather strips, etc. Regarding. [Prior Art] Generally, when a plasticizer is added to a vinyl chloride resin, a flexible molded product having appropriate elasticity can be obtained and is used in various fields. [Problems to be solved by the invention] However, molded products made from general soft vinyl chloride resin compositions have large compression set and poor restoring force after stress is applied. Small compression set is required for injection molded products such as gaskets and grommets, automotive products such as weather strips, door glass runs, and gaskets obtained by extrusion molding. Its use is restricted to certain applications. As a means to solve this technical problem, a method using vinyl chloride resin with a high average degree of polymerization was proposed,
As disclosed in JP-A-54-80354, JP-A-56-79141, etc., a method using a partially cross-linked vinyl chloride resin having a gel content that is insoluble in tetrahydrofuran, or a method using JP-A-56-79141. −
As disclosed in JP-A No. 115342, JP-A-59-51933, etc., a composition in which a partially crosslinked acrylonitrile-butadiene copolymer having a gel content that is insoluble in methyl ethyl ketone is blended with a vinyl chloride resin. Depending on the method of using things, etc.
It is generally known that compression set can be improved to some extent, but
The compression set is large compared to EPDM, NBR, chloroprene rubber, etc., and its applications are actually limited. The present invention is applicable to molded products such as packing and grommets obtained by injection molding general soft vinyl chloride resin compositions, weather strips obtained by extrusion molding, automobile parts such as door glass runs, gaskets, etc. Problems such as the large compression set of molded products, which limits their applications, and the use of highly polymerized vinyl chloride resins or partially crosslinked vinyl chloride resins with a gel content that is insoluble in tetrahydrofuran, or the use of these vinyl chloride resins. By using a soft vinyl chloride resin composition that is a blend of a partially crosslinked acrylonitrile-butadiene copolymer with a gel content that is insoluble in methyl ethyl ketone, the compression set of the resulting molded product is equal to that of a normal vinyl chloride resin composition. Although it is improved compared to molded products obtained from materials, its physical properties such as compression set are inferior compared to EPDM, NBR, and chloroprene rubber vulcanized with sulfur or organic peroxides, and its applications are limited. It was done to solve a problem. [Means for Solving the Problems] The present invention provides 100 parts of vinyl chloride resin (parts by weight,
For vehicles, the molded product obtained by molding a vinyl chloride resin composition comprising (the same applies hereinafter) and 20 to 200 parts of a plasticizer is heat-treated at a temperature of 50 to 120°C for 20 minutes to 24 hours. The present invention relates to a method for manufacturing an injection molded product or an extrusion molded product. [Example] The vinyl chloride resin used in the present invention is a vinyl chloride resin obtained by homopolymerizing a vinyl chloride monomer, or a vinyl chloride resin whose main component is vinyl chloride, i.e.
A vinyl chloride copolymer resin containing 85% (by weight, the same shall apply hereinafter) or more, and specific examples of the latter include vinyl chloride-vinyl acetate copolymer resin, vinyl chloride-ethylene copolymer resin, and vinyl chloride-propylene copolymer resin. Polymer resin, copolymer resin of vinyl chloride and acrylic acid or its ester, copolymer resin of vinyl chloride and methacrylic acid or its ester,
Examples include, but are not limited to, copolymer resins of vinyl chloride and alkyl vinyl ether. These vinyl chloride copolymer resins may be blended in a subordinate amount (up to 30%) to the vinyl chloride resin. As the vinyl chloride resin used in the present invention, JP-A-56-81325 other than the above vinyl chloride resin
Publication No. 1981-81328, Japanese Patent Application Laid-Open No. 1987-81328
A partially crosslinked vinyl chloride resin having a gel content that is insoluble in tetrahydrofuran as disclosed in Japanese Patent No. 195711 may also be used. The plasticizer used in the present invention is added to soften the resin composition used in the present invention,
The amount added is 20 to 200 per vinyl chloride resin.
parts, preferably 30 to 160 parts. The amount added is
If the amount is less than 20 parts, the molded product will not be sufficiently softened, and the effect of reducing permanent deformation due to heat treatment, that is, the development of rubber-like properties, will not occur. On the other hand, if the amount exceeds 200 parts, it becomes difficult to dry up, and the molded product becomes sticky after injection molding or extrusion molding, which is undesirable since there are problems in terms of processing and practical use. Examples of the plasticizers include phthalic acid plasticizers such as dioctyl phthalate, dinonyl phthalate, and diisodecyl phthalate, fatty acid plasticizers such as dioctyl adipate and dioctyl azelaate, trimellitic acid plasticizers such as trioctyl trimellitate, and polyesters. These include plasticizers commonly used in soft vinyl chloride resin compositions, such as epoxidized products such as epoxidized soybean oil, phosphoric acid plasticizers such as tricresyl phosphate, and chlorinated paraffin. It may be used or two or more types may be used in combination, and they can be used without particular limitation. In the present invention, a vinyl chloride resin composition is prepared from a vinyl chloride resin and a plasticizer.
Rubber substances may also be added. Examples of such rubber materials include acrylonitrile-butadiene copolymer, ethylene-vinyl acetate copolymer, ethylene-vinyl acetate-carbon monoxide terpolymer, chlorinated polyethylene, thermoplastic polyurethane, thermoplastic polyester, Examples include chloroprene rubber and acrylic rubber.
Among these rubber substances, JP-A-59-51933
As disclosed in the publication, the solubility in methyl ethyl ketone is 90% or less, and during its production, a polyfunctional monomer such as divinylbenzene is added to the polymerization system to create a crosslinked structure in the molecule. Acrylonitrile-butadiene copolymer is particularly preferred since it has the effect of reducing compression set. The rubber substances may be used alone or in combination of two or more, and the amount used is preferably 150 parts or less per 100 parts of the vinyl chloride resin. If the amount exceeds 150 parts, processability tends to deteriorate and the unique properties of vinyl chloride resins, such as good heat aging resistance, ozone resistance, and mechanical properties, tend to be lost. This is not desirable because it does things like this. In addition, heat stabilizers, fillers, lubricants,
Ultraviolet absorbers, pigments, blowing agents such as azodicarbonamide, processing aids such as copolymers of methyl methacrylate and butyl acrylate, and the like may be blended and used. The types and amounts of subcomponents used as necessary may be appropriately selected and used within a range that satisfies the above ratios depending on the purpose. The resin composition used in the present invention is mixed, kneaded, and granulated in the same steps as conventional soft vinyl chloride resin compositions, and can be molded by injection molding, extrusion molding, or the like. That is, they can be mixed together with a stabilizer, if necessary, using a mixer such as a super mixer or a ribbon blender, and the mixture is kneaded and granulated using a Banbury mixer, mixing roll, extruder, or the like. The granulated pellets are molded by a method such as press molding, injection molding, or extrusion molding, and the resulting molded product is heated at a temperature of 50 to 120°C, preferably 50 to 110°C for 20 minutes or more, preferably 1 hour or more. Heat treatment significantly reduces the permanent set of the molded product, especially the compression set. For heat treatment of the molded article, it is sufficient to simply leave it in a heating furnace such as a hot air dryer. The heat treatment temperature is 50℃
If it is less than 120°C, the permanent set, especially the compression set, will not be improved, and if it exceeds 120°C, the molded product will deform and become unable to hold its shape, which is not preferable. Moreover, if the heat treatment time is less than 20 minutes, it becomes impossible to reduce the compression set. The method of the present invention will be explained below based on Examples, but the present invention is not limited thereto. In addition, each physical property in an Example was measured by the following method. (Gel content insoluble in tetrahydrofuran) Extracted with hot tetrahydrofuran for 22 hours using a Soxhlet extractor, and measured the extracted residue separated with a 350 mesh filter. (Solubility of NBR in methyl ethyl ketone (hereinafter referred to as MEK)) 1 g of block-like NBR was added to 100 ml of MEK at 25°C.
Soak for an hour and measure the percentage of solution and particles that pass through a 100-mesh filter. (Compression set of molded product) Test pieces for measuring compression set were made using the following three processing methods, and the compression set of the molded product was measured. (1) How to make press-formed products and measurement methods Dry blends of each formulation shown in Table 1 were rolled at a temperature of 160℃ (175℃ for formulations 2 and 3).
Knead for 7 minutes to make a masticated sheet with a thickness of about 3 mm, overlap the resulting sheets and make a 170 mm
℃ (180℃ for formulations 2 and 3) for 4 minutes, then 170℃ (180℃ for formulations 2 and 3)
For 3 minutes, apply a load of 150Kg/cm 2 to a thickness of 12.7
A press plate of 29.0 mm in diameter was made, hollowed out into a right cylinder shape with a diameter of 29.0 mm, and heat treated under the conditions shown in Table 2.
Compliant with 6301, compression rate 25%, compression condition 70℃
Measurement of compression set after 22 hours. (2) How to make and measure injection molded products A masticated sheet with a thickness of about 3 mm was prepared using each compounding system shown in Table 1 in the same manner and under the same conditions as above, and the resulting sheet was divided into approximately 3 mm squares. Cut into pellets, use the pellets to apply mold clamping pressure of 150 tons,
With an injection molding machine with an injection capacity of 173 cm 3 /shot,
Using a mold with a thickness of 12 mm, length of 50 mm, and width of 100 mm, the cylinder temperature was 165°C (180°C for composition 3).
Nozzle temperature 160℃ (175℃ for formulation 3),
Injection molding was performed at an injection pressure of 50 Kg/cm 2 . A right cylindrical object with a diameter of 29.0 mm was cut out from the obtained molded plate, and heat treated under the conditions shown in Table 3 to obtain JIS K.
Compliant with 6301, compression ratio 25%, compression condition 22 at 70℃
Measure the compression set after time. (3) How to make and measure extrusion molded products The same method as above was used for the formulation 3 shown in Table 1.
A masticated sheet with a thickness of approximately 3 mm was prepared under the following conditions.
The obtained sheet was cut into approximately 3 mm squares to make pellets, and the pellets were used with a full flight screw with L/D = 22 and compression ratio of 3.0.
Extrude the profile extrusion molded product (sealing member for automobiles) (1) shown in Figure 1 using a 50 mm single screw extruder, and
Heat treated under the conditions shown in the table, and the molded product was JIS K certified using the apparatus 2 having the spacer 3 shown in Fig. 2.
It was measured using the same method as the compression set measurement method for 6301. The compression rate was 53%, the compression conditions were 70℃ for 22 hours, and the extrusion molding conditions were cylinder temperatures from the hopper side: C 1 150℃, C 2 160℃, C 3 170℃,
The C 4 temperature was set at 175°C, the die temperature was set at 175°C, and the screw rotation speed was 30 rpm. (Appearance after heat treatment) The press molded, injection molded, and extrusion molded products described above were placed in a hot air dryer and heat treated under the heat treatment conditions shown in Tables 2, 3, and 4. The change in gloss was observed and evaluated based on the following criteria. ○: No change △: Small change ×: Large change Examples 1 to 6 and Comparative Examples 1 to 2 The formulations shown in Table 1 were roll kneaded, a press molded product was produced from the resulting masticated sheet, and the The molded product was placed in a hot air dryer under the heat treatment conditions shown in Table 2, and the appearance after heat treatment was observed.
Compression set was measured in accordance with K 6301. The results are shown in Table 2. Note that S 1003 and S3000 in Table 1 are Kanevinyl S1003 (=
1300) and Kanevinyl S3000 (3200), partially crosslinked vinyl chloride resin has THF insoluble content of 19%, acrinitrile-butadiene copolymer has acrinitrile content of 33%, MEK solubility 21%, Moony Acrynitrile-butadiene copolymer with a viscosity of 50, DOP is dioctyl phthalate.

【表】【table】

【表】 第2表の結果から配合1のものは熱処理温度23
℃で24時間での圧縮永久歪は60%であるが、熱処
理温度50℃で熱処理時間が長くなるにつれ圧縮永
久歪は57、54、43%と改善され、熱処理温度が
130℃で1時間での圧縮永久歪は改良されず、成
形品の外観が変化した。また配合2、3のもので
も同じ傾向を示していることがわかる。とくに配
合3のもので熱処理温度50℃、70℃で24時間処理
すると、圧縮永久歪は各々29%、25%と大巾に改
善することがわかる。 実施例7〜10および比較例3〜4 第1表の配合1、3の配合物を用いてペレツト
を作製し、前記射出条件で射出成形した成形品を
第3表の熱処理条件にて熱風乾燥機にて処理した
のち外観を観察するとともに、JIS K 6301に準
拠して圧縮永久歪を測定した。結果を第3表に示
す。
[Table] From the results in Table 2, the heat treatment temperature for formulation 1 is 23
The compression set in 24 hours at ℃ is 60%, but as the heat treatment temperature increases and the heat treatment time increases, the compression set improves to 57, 54, and 43%, and the heat treatment temperature increases.
Compression set at 130°C for 1 hour was not improved, and the appearance of the molded product changed. It can also be seen that formulations 2 and 3 show the same tendency. In particular, it can be seen that when Blend 3 is heat treated at a heat treatment temperature of 50°C and 70°C for 24 hours, the compression set is significantly improved to 29% and 25%, respectively. Examples 7 to 10 and Comparative Examples 3 to 4 Pellets were prepared using the formulations 1 and 3 in Table 1, and the molded products injection molded under the above injection conditions were hot-air dried under the heat treatment conditions in Table 3. After processing in a machine, the appearance was observed and the compression set was measured in accordance with JIS K 6301. The results are shown in Table 3.

【表】 第3表の結果から、配合1のものでは熱処理温
度23℃で24時間での圧縮永久歪が59%であるが、
50℃で24時間熱処理すると49%となり、70℃では
熱処理1時間で52%、24時間で46%と改善される
ことがわかる。しかし130℃で1時間、では圧縮
永久歪は62%と大きく、成形品の外観も変化する
ことがわかる。一方、配合3の配合物を用いて作
つた射出成形品は熱処理条件が23℃で24時間、
130℃で1時間では圧縮永久歪は各々47%、48%
であるが、70℃で1時間および24時間熱処理する
と圧縮永久歪はそれぞれ35%、27%と大巾に改良
されることがわかる。 実施例11〜14および比較例5〜6 第1表の配合3の配合物を用いてペレツトを作
製し、前記押出条件で第1図に示した自動車用シ
ール部材の形状に押出し、該成形品を第4表の熱
処理条件にて熱風乾燥機にて熱処理し、第2図に
示した装置を用いて圧縮永久歪を測定した。結果
を第4表に示す。
[Table] From the results in Table 3, the compression set of formulation 1 after 24 hours at a heat treatment temperature of 23°C is 59%;
It can be seen that when heat treated at 50°C for 24 hours, the improvement was 49%, and at 70°C, the improvement was 52% after 1 hour of heat treatment and 46% after 24 hours. However, when heated at 130°C for 1 hour, the compression set was as large as 62%, and the appearance of the molded product also changed. On the other hand, the injection molded product made using the formulation 3 was heat treated at 23℃ for 24 hours.
Compression set at 130℃ for 1 hour is 47% and 48%, respectively.
However, it can be seen that when heat treated at 70°C for 1 hour and 24 hours, the compression set was significantly improved to 35% and 27%, respectively. Examples 11 to 14 and Comparative Examples 5 to 6 Pellets were prepared using the formulation 3 in Table 1, and extruded under the extrusion conditions into the shape of the automotive sealing member shown in Figure 1. were heat treated in a hot air dryer under the heat treatment conditions shown in Table 4, and the compression set was measured using the apparatus shown in FIG. The results are shown in Table 4.

【表】【table】

【表】 第4表の結果から、熱処理条件が23℃で24時
間、130℃で1時間での圧縮永久歪は各々58%、
59%であるが、熱処理条件が50℃で24時間、70℃
で24時間熱処理すると圧縮永久歪は各々43%、40
%と大巾に改善されることがわかる。 [発明の効果] 本発明に用いる樹脂組成物をプレス成形、射出
成形、押出成形などの方法により成形加工し、そ
の成形品を本発明の方法により熱処理すると該成
形品の圧縮永久歪を大巾に改善することができ、
イオウや有機過酸化物で加硫したEPDM、
NBR、クロロプレンゴムなどと同等の永久歪の
成形品がえられる。
[Table] From the results in Table 4, the compression set under heat treatment conditions of 23℃ for 24 hours and 130℃ for 1 hour is 58%,
59%, but the heat treatment conditions are 50℃ for 24 hours and 70℃
When heat treated for 24 hours, the compression set was 43% and 40%, respectively.
It can be seen that there is a significant improvement of %. [Effect of the invention] When the resin composition used in the present invention is molded by a method such as press molding, injection molding, or extrusion molding, and the molded product is heat-treated by the method of the present invention, the compression set of the molded product can be significantly reduced. can be improved,
EPDM vulcanized with sulfur or organic peroxide,
Molded products with permanent deformation equivalent to NBR, chloroprene rubber, etc. can be obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は塩化ビニル形樹脂成形物の圧縮永久歪
を評価するための自動車部品用シール部材の押出
成形品の断面説明図、第2図は第1図に示す試験
片を用いて圧縮永久歪を測定している状態を示す
説明図である。 (図面の主要符号)、1:異形押出成形品。
Figure 1 is a cross-sectional explanatory diagram of an extrusion molded product of a sealing member for automobile parts for evaluating the compression set of a vinyl chloride type resin molded product, and Figure 2 is a cross-sectional diagram of an extrusion molded product of a sealing member for automobile parts for evaluating the compression set of a vinyl chloride type resin molded product. FIG. 2 is an explanatory diagram showing a state in which . (Main symbols in the drawing), 1: Profile extrusion molded product.

Claims (1)

【特許請求の範囲】[Claims] 1 塩化ビニル系樹脂100重量部および可塑剤20
〜200重量部よりなる塩化ビニル系樹脂組成物か
ら成形加工してえられた成形品を50〜120℃の温
度で20分〜24時間加熱処理することを特徴とする
車輌用の射出成形品または押出成形品の製造方
法。
1 100 parts by weight of vinyl chloride resin and 20 parts by weight of plasticizer
An injection molded product for a vehicle, characterized in that a molded product obtained by molding a vinyl chloride resin composition comprising ~200 parts by weight is heat-treated at a temperature of 50 to 120°C for 20 minutes to 24 hours. Method for manufacturing extruded products.
JP60053020A 1985-03-15 1985-03-15 Method of reducing size of permanent strain of vinyl chloride series resin molded product Granted JPS61211021A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60053020A JPS61211021A (en) 1985-03-15 1985-03-15 Method of reducing size of permanent strain of vinyl chloride series resin molded product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60053020A JPS61211021A (en) 1985-03-15 1985-03-15 Method of reducing size of permanent strain of vinyl chloride series resin molded product

Publications (2)

Publication Number Publication Date
JPS61211021A JPS61211021A (en) 1986-09-19
JPH056502B2 true JPH056502B2 (en) 1993-01-26

Family

ID=12931214

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60053020A Granted JPS61211021A (en) 1985-03-15 1985-03-15 Method of reducing size of permanent strain of vinyl chloride series resin molded product

Country Status (1)

Country Link
JP (1) JPS61211021A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0493233A (en) * 1990-08-08 1992-03-26 Mitsubishi Kasei Vinyl Co Improvement of permanent compressive strain of polyvinyl chloride-based resin molded article
JPH06102365B2 (en) * 1991-02-27 1994-12-14 豊田合成株式会社 Manufacturing method for long molded products
US5489404A (en) * 1994-08-08 1996-02-06 General Electric Company Process for annealing thermoplastics

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5065563A (en) * 1973-10-12 1975-06-03
JPS59182834A (en) * 1983-03-31 1984-10-17 Kanegafuchi Chem Ind Co Ltd Automobile part

Also Published As

Publication number Publication date
JPS61211021A (en) 1986-09-19

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