Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0657758B2 - Manufacturing method of soft vinyl chloride foam moldings with small permanent set - Google Patents
[go: Go Back, main page]

JPH0657758B2 - Manufacturing method of soft vinyl chloride foam moldings with small permanent set - Google Patents

Manufacturing method of soft vinyl chloride foam moldings with small permanent set

Info

Publication number
JPH0657758B2
JPH0657758B2 JP61214689A JP21468986A JPH0657758B2 JP H0657758 B2 JPH0657758 B2 JP H0657758B2 JP 61214689 A JP61214689 A JP 61214689A JP 21468986 A JP21468986 A JP 21468986A JP H0657758 B2 JPH0657758 B2 JP H0657758B2
Authority
JP
Japan
Prior art keywords
vinyl chloride
parts
molded product
chloride resin
soft 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 - Fee Related
Application number
JP61214689A
Other languages
Japanese (ja)
Other versions
JPS6369838A (en
Inventor
一正 山根
正三 正国
以佐夫 竹下
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.)
Kaneka Corp
Original Assignee
Kaneka Corp
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 Kaneka Corp filed Critical Kaneka Corp
Priority to JP61214689A priority Critical patent/JPH0657758B2/en
Publication of JPS6369838A publication Critical patent/JPS6369838A/en
Priority to JP5233221A priority patent/JPH0774286B2/en
Publication of JPH0657758B2 publication Critical patent/JPH0657758B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、成形品の発泡倍率が1.2〜3.5倍であり、しか
も、永久歪の小さい特定の軟質塩化ビニル系樹脂組成物
からなる発泡成形品の製法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a foam molding which comprises a specific soft vinyl chloride resin composition having a foaming ratio of 1.2 to 3.5 times and a small permanent set. Regarding the manufacturing method of goods.

[従来の技術] 従来より、軟質塩化ビニル系製品の軽量化および遮音
性、断熱性、シール性などの向上を目的として塩化ビニ
ル系樹脂に可塑剤を添加した、いわゆる軟質塩化ビニル
系樹脂組成物からの発泡成形品が製造され、使用されて
いるが、緻密で均一な独立発泡セルを有し、発泡倍率が
1.2倍以上で、しかも、永久歪が小さい軟質塩化ビニル
系発泡成形品はえられておらず、限定された範囲でしか
使用されていない。
[Prior Art] Conventionally, a so-called soft vinyl chloride resin composition obtained by adding a plasticizer to a vinyl chloride resin for the purpose of reducing the weight of a soft vinyl chloride product and improving sound insulation, heat insulation and sealing properties. Although the foamed molded product from is manufactured and used, it has dense and uniform independent foamed cells, and the expansion ratio is
A flexible vinyl chloride foamed molded product that is 1.2 times or more and has a small permanent set has not been obtained, and is used only in a limited range.

塩化ビニル系発泡成形品を製造する方法としては、押出
発泡成形法、射出成形法、カレンダー成形法などがあ
り、また蒸発型発泡剤を使用して製造する方法と分解型
発泡剤を使用して製造する方法とがある。
As a method for producing a vinyl chloride-based foam molded article, there are an extrusion foam molding method, an injection molding method, a calender molding method, and the like, and a method of manufacturing using an evaporation type foaming agent and a decomposition type foaming agent. There is a manufacturing method.

押出発泡成形法により分解型発泡剤を使用して製造する
方法は、従来から使用されている押出機を若干改造する
だけで転用でき、しかもプロセスが簡単であるという利
点があるため、低発泡〜中発泡成形品の製造に多用され
ている。とくに、この押出発泡成形法の分野では、永久
歪や発泡倍率、発泡セルの均一性の他、押出形状が安定
し、成形品の表面が平滑で外観の良好な成形品が求めら
れているが、このような発泡成形品はえられていない。
The method of producing by using the decomposition type foaming agent by the extrusion foaming molding method has the advantage that it can be diverted by slightly modifying the conventionally used extruder and has the advantage that the process is simple. It is often used in the production of medium-foam molded products. In particular, in the field of this extrusion foam molding method, in addition to the permanent set, the expansion ratio, the uniformity of the foam cells, the extrusion shape is stable, and the molded product has a smooth surface and a good appearance. , Such foam-molded products have not been obtained.

このような発泡成形品の発泡倍率、発泡セルの均一性、
押出成形における成形性などの問題を解決しようとする
とき、加工性改良剤の添加が一般に採用される方法であ
り、この方法がある程度有効であることはよく知られて
いる。たとえば、特開昭51-5371号、特開昭58-52327号
の各公報に示されているように、まずシートを成形した
のち発泡炉中で発泡を行なう、いわゆる二段発泡法で
は、発泡成形品の発泡倍率、発泡セルの均一性などを改
良するという点ではその効果が認められている。しか
し、一般の押出発泡成形では、その効果は認められな
い。
Foaming ratio of such foamed molded product, uniformity of foamed cells,
When trying to solve problems such as moldability in extrusion molding, the addition of a processability improver is a generally adopted method, and it is well known that this method is effective to some extent. For example, as disclosed in JP-A-51-5371 and JP-A-58-52327, in the so-called two-stage foaming method in which a sheet is first molded and then foamed in a foaming furnace, Its effect has been recognized in terms of improving the expansion ratio of a molded product, the uniformity of foam cells, and the like. However, the effect is not recognized in general extrusion foam molding.

すなわち、一般の押出発泡成形法では、一般に使用され
ているメタクリル酸メチルを主成分とする共重合体で、
比粘度が1〜2の加工性改良剤を添加しても、緻密で均
一な独立発泡セルを有し、発泡倍率が1.2倍以上で、表
面平滑性が極めて良好な発泡成形品をうることはできな
い。また、射出成形法などでも、前記の比粘度が1〜2
の加工性改良剤の添加では、発泡倍率が1.2以上で、か
つ緻密で均一な独立発泡セルを有する発泡成形品はえら
れない。
That is, in a general extrusion foam molding method, a commonly used copolymer containing methyl methacrylate as a main component,
Even if a processability improver having a specific viscosity of 1 to 2 is added, it is possible to obtain a foamed molded product having a dense and uniform independent foam cell, a foaming ratio of 1.2 times or more, and an extremely good surface smoothness. Can not. In addition, even in the injection molding method, the specific viscosity is 1 to 2
With the addition of the processability improver, a foamed molded product having a foaming ratio of 1.2 or more and having dense and uniform closed cells cannot be obtained.

一方、特開昭61-66732号公報に示されているように、永
久歪を小さくする目的で部分架橋のアクリロニトリル−
ブタジエンゴムを添加した軟質塩化ビニル系樹脂組成物
に分解型発泡剤を添加して押出発泡成形すると、永久歪
は小さくなるが、発泡倍率が上りにくく、均一な発泡セ
ルがえられないという問題はより顕著に現れる。
On the other hand, as disclosed in JP-A-61-66732, a partially cross-linked acrylonitrile-containing compound is used for the purpose of reducing permanent set.
When extrusion-foam molding is performed by adding a decomposable foaming agent to a soft vinyl chloride resin composition containing butadiene rubber, the permanent strain becomes small, but the expansion ratio is difficult to increase, and the problem that uniform foam cells cannot be obtained Appears more prominently.

[発明が解決しようとする問題点] 本発明は、各種発泡成形法によって軟質塩化ビニル系樹
脂組成物発泡成形品をえようとする際、従来の技術では
発泡成形品の発泡状態を緻密で均一な独立発泡セル状態
にし、発泡倍率を1.2倍以上にし、しかも、永久歪を小
さくした発泡成形品をうることができず、限定された範
囲でしか使用されていないという問題を解決するために
なされたものである。
[Problems to be Solved by the Invention] According to the present invention, when a flexible vinyl chloride resin composition foam-molded article is obtained by various foam-molding methods, the foaming state of the foam-molded article is dense and uniform according to the conventional technique. It is made to solve the problem that it is used only in a limited range because it is not possible to obtain a foamed molded product in which it is made into an independent foam cell state, the expansion ratio is 1.2 times or more, and the permanent set is small. It is a thing.

[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)に対して、メタクリル酸メチルを主成分とする共重
合体0.4gを含む100mlのベンゼン溶液の30℃で測定した
比粘度が2.5以上のメタクリル酸メチル系共重合体1〜3
0部、可塑剤20〜200部および発泡剤0.5〜10部を含む発
泡用軟質塩化ビニル系樹脂組成物を発泡成形してえられ
た成形品を40〜120℃の温度で20分間以上加熱処理する
ことを特徴とする発泡倍率1.2〜3.5倍で永久歪の小さい
軟質塩化ビニル系発泡成形品の製法に関する。
[Means for Solving Problems] The present invention is based on 100 parts of vinyl chloride resin (parts by weight, the same applies hereinafter) and 100 ml of a benzene solution containing 0.4 g of a copolymer containing methyl methacrylate as a main component. Methyl methacrylate-based copolymers 1-3 with a specific viscosity of 2.5 or higher measured at 30 ℃
A molded product obtained by foam molding a soft vinyl chloride resin composition for foaming containing 0 part, 20 to 200 parts of a plasticizer and 0.5 to 10 parts of a foaming agent is heat treated at a temperature of 40 to 120 ° C for 20 minutes or more. The present invention relates to a method for producing a soft vinyl chloride foamed molded product having a foaming ratio of 1.2 to 3.5 and a small permanent set.

[実施例] 本発明に使用す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樹脂または85%(重
量%、以下同様)以上塩化ビニルを含有する塩化ビニル
系共重合体のことであり、ゲル分を含有する部分架橋塩
化ビニル系樹脂などであってもよく、前記規定に適合す
るかぎり、従来から知られているいかなる塩化ビニル系
樹脂であっても使用しうる。
[Example] The vinyl chloride resin used in the present invention means a vinyl chloride resin obtained by homopolymerizing a vinyl chloride monomer or a vinyl chloride copolymer containing 85% (% by weight, the same hereinafter) of vinyl chloride or more. That is, a partially cross-linked vinyl chloride resin containing a gel component may be used, and any conventionally known vinyl chloride resin may be used as long as it meets the above regulations.

85%以上塩化ビニルを含有する塩化ビニル共重合体の塩
化ビニル以外の共重合体成分としては、たとえば酢酸ビ
ニル、ステアリン酸ビニルなどのビニルエステル類、エ
チレン、プロピレンなどのオレフィン類、(メタ)アク
リル酸ブチル、(メタ)アクリル酸−2−エチルヘキシ
ルなどの(メタ)アクリル酸エステル類、マレイン酸ブ
チル、マレイン酸オクチルなどのマレイン酸エステル
類、フマル酸ブチル、フマル酸オクチルなどのフマル酸
エステル類、あるいはこれらの酸などが例示されるが、
これらに限定されるものではない。これら塩化ビニル以
外の成分は2種以上併用してもよい。
Examples of the copolymer component other than vinyl chloride in the vinyl chloride copolymer containing 85% or more vinyl chloride include vinyl esters such as vinyl acetate and vinyl stearate, olefins such as ethylene and propylene, and (meth) acryl. Butyl acid, (meth) acrylic acid esters such as 2-ethylhexyl (meth) acrylate, maleic acid esters such as butyl maleate and octyl maleate, fumaric acid esters such as butyl fumarate and octyl fumarate, Alternatively, these acids and the like are exemplified,
It is not limited to these. Two or more of these components other than vinyl chloride may be used in combination.

また、ゲル分を含有する部分架橋塩化ビニル系樹脂とし
ては、たとえば架橋剤として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(メタ)ア
クリレート、1,2−ポリブタジエン類などの多官能性
化合物を使用した共重合によってえられる樹脂などが例
示されるが、これらに限定されるものではない。
As the partially crosslinked vinyl chloride resin containing a gel component, for example, a polyfunctional compound such as diallyl phthalate, diallyl maleate, polyethylene glycol di (meth) acrylate, or 1,2-polybutadiene is used as a crosslinking agent. Examples thereof include resins obtained by copolymerization, but are not limited to these.

これらの塩化ビニル系樹脂は2種以上併用してもよく、
またその併用割合も目的に応じて自由に選択しうる。
Two or more of these vinyl chloride resins may be used in combination,
Further, the combination ratio can be freely selected according to the purpose.

塩化ビニル系樹脂の平均重合度は600〜4500であること
が好ましく、1000〜3200のものがとくに好ましい。平均
重合度が600未満のばあいには、可塑剤を混合する際に
ドライアップさせることが困難であり、また成形品の永
久歪が大きくなり好ましくない傾向にある。一方、平均
重合度が4500をこえると、充分にゲル化させることが困
難となる傾向にある。
The average degree of polymerization of the vinyl chloride resin is preferably 600 to 4500, and particularly preferably 1000 to 3200. When the average degree of polymerization is less than 600, it is difficult to dry up the plasticizer when it is mixed, and the permanent set of the molded article becomes large, which is not preferable. On the other hand, when the average degree of polymerization exceeds 4,500, it tends to be difficult to sufficiently gelate.

本発明に使用するメタクリル酸メチル系共重合体とは、
メタクリル酸メチルを主成分として、すなわち50〜95%
含有し、これとアクリル酸エステルおよび(または)メ
タクリル酸エステル(メタクリル酸メチルを除く)およ
び(または)少量の架橋剤との共重合体あるいはグラフ
ト共重合体である。
The methyl methacrylate-based copolymer used in the present invention,
Mainly methyl methacrylate, ie 50-95%
It is a copolymer or graft copolymer of an acrylic acid ester and / or a methacrylic acid ester (excluding methyl methacrylate) and / or a small amount of a crosslinking agent contained therein.

該メタクリル酸メチル系共重合体の分子量は、該共重合
体0.4gを含む100mlのベンゼン溶液の30℃で測定した比
粘度が2.5以上、好ましくは2.5〜6.0となるような高分
子量のものであり、さらに好ましくはガラス転移温度が
85℃以下のものである。該比粘度が2.5未満のばあいに
は、発泡成形品のセルの均一性、独立性、押出成形品の
表面平滑性などが改良されず、また発泡倍率も大きくな
らず、好ましくない。また、ペレットコンパウンド製造
時の混練性を改良するためには、ガラス転移温度が85℃
以下であるのが好ましい。
The molecular weight of the methyl methacrylate copolymer is such that the specific viscosity of 100 ml of a benzene solution containing 0.4 g of the copolymer measured at 30 ° C. is 2.5 or more, preferably 2.5 to 6.0. And more preferably has a glass transition temperature
It is below 85 ℃. When the specific viscosity is less than 2.5, the uniformity and independence of cells of the foam-molded product, the surface smoothness of the extrusion-molded product, and the like are not improved, and the expansion ratio does not increase, which is not preferable. In addition, in order to improve the kneading properties during the production of pellet compounds, the glass transition temperature should be 85 ° C.
The following is preferable.

本発明に使用するメタクリル酸メチル系共重合体は、塩
化ビニル系樹脂100部に対して1〜30部、好ましくは3
〜25部、とくに好ましくは5〜20部使用される。該使用
量が1部未満では充分な発泡倍率向上効果が生じず、逆
に30部をこえると、成形品が硬くなって柔軟性がなくな
り、またコストも高くなり、好ましくない。なお、メタ
クリル酸メチル系共重合体は、2種以上併用してもよ
い。
The methyl methacrylate-based copolymer used in the present invention is 1 to 30 parts, preferably 3 to 100 parts of vinyl chloride resin.
.About.25 parts, particularly preferably 5 to 20 parts are used. If the amount used is less than 1 part, a sufficient effect of improving the expansion ratio does not occur. On the contrary, if it exceeds 30 parts, the molded product becomes hard and inflexible, and the cost increases, which is not preferable. Two or more methyl methacrylate copolymers may be used in combination.

本発明に使用する可塑剤は、成形品に柔軟性、ゴム触感
などを与えるために添加されるものであり、その具体例
としては、たとえばジブチルフタレート、ジオクチルフ
タレート、ジイソデシルフタレート、ジイソノニルフタ
レート、ジウンデシルフタレート、トリオクチルトリメ
リテート、トリイソオクチルトリメリテートなどの芳香
族多塩基酸のアルキルエステル、ジブチルアジペート、
ジオクチルアジペート、ジイソノニルアジペート、ジブ
チルアゼレート、ジオクチルアゼレート、ジイソノニル
アゼレートなどの脂肪族多塩基酸のアルキルエステル、
トリクレジルホスフェートなどのリン酸アルキルエステ
ル、さらにはポリエステル系可塑剤、エポキシ系可塑
剤、塩素化パラフィンなどの通常使用される可塑剤があ
げられる。これらは単独で用いてもよく、2種以上併用
してもよい。
The plasticizer used in the present invention is added in order to give the molded article flexibility, rubber feel, and the like, and specific examples thereof include dibutyl phthalate, dioctyl phthalate, diisodecyl phthalate, diisononyl phthalate, diundecyl. Alkyl ester of aromatic polybasic acid such as phthalate, trioctyl trimellitate, triisooctyl trimellitate, dibutyl adipate,
Alkyl ester of aliphatic polybasic acid such as dioctyl adipate, diisononyl adipate, dibutyl azelate, dioctyl azelate, diisononyl azelate,
Examples include phosphoric acid alkyl esters such as tricresyl phosphate, and commonly used plasticizers such as polyester plasticizers, epoxy plasticizers and chlorinated paraffins. These may be used alone or in combination of two or more.

可塑剤は塩化ビニル系樹脂100部に対して20〜200部、好
ましくは30〜160部使用される。該使用量が200部をこえ
ると、成形品の耐熱変形性、セルの独立性が低下して好
ましくなく、一方、20部未満では成形品に柔軟性、ゴム
触感などを与えることができなくなり、好ましくない。
The plasticizer is used in an amount of 20 to 200 parts, preferably 30 to 160 parts, per 100 parts of vinyl chloride resin. If the amount used exceeds 200 parts, the heat distortion resistance of the molded product and the independence of the cells decrease, which is not preferable. On the other hand, if it is less than 20 parts, the molded product cannot be imparted with flexibility, rubber touch, etc. Not preferable.

本発明に使用する発泡剤としては、たとえばバリウムア
ゾジカルボキシレート、ヒドラゾジカルボンアミド、ア
ゾジカルボンアミド、4,4′−オキシビスベンゼンスル
ホニルセミカルバジド、N,N′−ジメチル−N,N′−ジニ
トロソテレフタルアミド、N,N′−ジニトロソペンタメ
チレンテトラミン、p−トルエンスルホニルヒドラジ
ド、ベンゼン−1,3−ジスルホニルヒドラジド、ジフェ
ニルスルホン−3,3′−ジスルホニルヒドラジド、p−
トルエンスルホニルセミカルバジドなどがあげられる。
これらは単独で用いてもよく、2種以上を適宜選択して
併用してもよい。
Examples of the foaming agent used in the present invention include barium azodicarboxylate, hydrazodicarbonamide, azodicarbonamide, 4,4′-oxybisbenzenesulfonyl semicarbazide, N, N′-dimethyl-N, N′-diene. Nitrosoterephthalamide, N, N'-dinitrosopentamethylenetetramine, p-toluenesulfonyl hydrazide, benzene-1,3-disulfonylhydrazide, diphenylsulfone-3,3'-disulfonylhydrazide, p-
Examples include toluenesulfonyl semicarbazide.
These may be used alone or in combination of two or more kinds as appropriate.

発泡剤は塩化ビニル系樹脂100部に対して0.5〜10部、好
ましくは1.5〜5部使用される。該使用量が、0.5部未満
では、発生するガス量が少ないため、発泡倍率が上がら
ず好ましくない。逆に、該使用量が10倍をこえると、過
発泡となってセルの破壊、連通が発生し、セルの均一
性、独立性が低下し、好ましくない。
The blowing agent is used in an amount of 0.5 to 10 parts, preferably 1.5 to 5 parts, per 100 parts of vinyl chloride resin. If the amount used is less than 0.5 part, the amount of gas generated is small, and the expansion ratio does not increase, which is not preferable. On the other hand, if the amount used exceeds 10 times, over-foaming may occur, resulting in breakage and communication of cells, and deterioration of cell uniformity and independence, which is not preferable.

本発明の方法により発泡成形品を製造する際には、必要
に応じて安定剤、滑剤、充填剤、紫外線吸収剤、顔料、
NBR、部分架橋NBR、クロロプレン、部分架橋クロロプレ
ンなどのゴム類、ポリウレタン系樹脂、ポリエステル系
樹脂、エチレン−酢酸ビニル共重合体、塩素化ポリエチ
レンなどの熱可塑性樹脂などを配合して使用してもよ
く、さらにキッカー剤、分解抑制剤、セル調節剤などの
発泡助剤を使用してもよく、その種類や添加量は、目的
に応じて適宜選択すればよい。
When producing a foam molded article by the method of the present invention, if necessary, stabilizer, lubricant, filler, ultraviolet absorber, pigment,
Rubbers such as NBR, partially crosslinked NBR, chloroprene, and partially crosslinked chloroprene, polyurethane-based resins, polyester-based resins, ethylene-vinyl acetate copolymer, thermoplastic resins such as chlorinated polyethylene may be blended and used. Further, a foaming aid such as a kicker agent, a decomposition inhibitor, a cell regulator and the like may be used, and the type and addition amount thereof may be appropriately selected according to the purpose.

本発明の方法により軟質塩化ビニル系発泡成形品を製造
する際には、たとえば一般の軟質塩化ビニル系樹脂組成
物を製造する工程を使用して成分をブレンド、ペレット
化し、ついで該ペレットを発泡成形し、ついでその成形
品を加熱処理すればよい。
When producing a soft vinyl chloride-based foamed molded article by the method of the present invention, the components are blended and pelletized by using, for example, the step of producing a general soft vinyl chloride-based resin composition, and then the pellets are foamed and molded. Then, the molded product may be heat-treated.

すなわち、ブレンドに際しては、ヘンシェルミキサー、
スーパーミキサー、リボンブレンダーなど従来から公知
のブレンダーを使用し、塩化ビニル系樹脂などの成分を
投入後、可塑剤を一括、断続または連続的に投入して80
〜150℃まで昇温して可塑剤をドライアップさせ、軟質
塩化ビニル系樹脂のパウダーコンパウンドを製造する。
この際、塩化ビニル系樹脂以外の成分の投入は、ドライ
アップさせたのちに投入したり、ドライアップさせる途
中で投入してもよい。
That is, when blending, use a Henschel mixer,
Using a conventionally known blender such as a super mixer or ribbon blender, add the components such as vinyl chloride resin and then add the plasticizer all at once, intermittently or continuously.
The temperature is raised to ~ 150 ° C to dry up the plasticizer and produce a soft vinyl chloride resin powder compound.
At this time, the components other than the vinyl chloride resin may be added after the dry-up, or may be added during the dry-up.

ついで、該混合物を加圧ニーダー、コニーダー、ミキシ
ングロール、各種押出機などに供給し、100〜200℃の温
度で混練りし、軟質塩化ビニル系樹脂組成物のペレット
コンパウンドが製造される。
Then, the mixture is supplied to a pressure kneader, a co-kneader, a mixing roll, various extruders and the like and kneaded at a temperature of 100 to 200 ° C. to produce a pellet compound of a soft vinyl chloride resin composition.

発泡成形法としては、押出成形法、射出成形法、カレン
ダー成形法など、従来一般に使用されている成形法が利
用できる。
As the foam molding method, a conventionally used molding method such as an extrusion molding method, an injection molding method or a calender molding method can be used.

押出発泡成形法により成形するばあいには、該ペレット
コンパウンドを成形品の目的に合わせた各種の形状をも
ったダイスを取付けた各種の単軸または二軸押出機を用
いた押出発泡成形法により軟質塩化ビニル系樹脂組成物
発泡成形品が製造される。押出発泡成形の際、金属、軟
質PVC、硬質PVCなどと共押出してもよい。
When molding by extrusion foam molding method, the pellet compound by extrusion foam molding method using various single-screw or twin-screw extruders with dies having various shapes according to the purpose of the molded product. A soft vinyl chloride resin composition foam-molded article is produced. During extrusion foam molding, it may be co-extruded with metal, soft PVC, hard PVC or the like.

押出発泡成形法における成形温度は、通常100〜200℃の
範囲で行なわれ、好ましくはダイスの温度をシリンダー
先端温度より低く設定し、しかもこの温度差を5℃以上
に保ちながら成形するのが好ましい。
The molding temperature in the extrusion foam molding method is usually in the range of 100 to 200 ° C., preferably, the temperature of the die is set lower than the temperature at the tip of the cylinder, and molding is preferably performed while maintaining this temperature difference at 5 ° C. or more. .

スクリュー形状にはとくに限定はなく、従来から使用さ
れている公知のスクリュー、たとえばダルメージ型、フ
ルフライト型などのものを使用しうる。該スクリューの
L/Dは15〜40であるものが好ましく、とくに15〜30の
ものが好ましい。また、スクリユーの圧縮比は、1.0〜
5.0であるものが好ましく、とくに1.5〜3.5のものが好
ましい。
The screw shape is not particularly limited, and a conventionally known screw such as a dullage type or full flight type screw can be used. The L / D of the screw is preferably from 15 to 40, more preferably from 15 to 30. The compression ratio of the screen is 1.0-
It is preferably 5.0, particularly preferably 1.5 to 3.5.

このようにして、押出成形、射出成形、カレンダー成形
などでえられた発泡倍率1.2〜3.5倍で、かつ緻密で均一
な独立発泡セルを有する発泡成形品を40〜120℃で20分
間以上加熱処理をすると、永久歪が著しく改良される。
このように加熱処理によって永久歪を著しく小さくする
方法は、今まで全く知られていない。
In this way, a foam-molded product with a foaming ratio of 1.2-3.5 times obtained by extrusion molding, injection molding, calender molding, etc. and having dense and uniform independent foam cells is heat treated at 40-120 ° C for 20 minutes or more. When set, the permanent set is remarkably improved.
Up to now, there is no known method for significantly reducing the permanent set by heat treatment.

発泡成形品の加熱処理は、40〜120℃で20分間以上加熱
処理するかぎり連続的に処理してもよく、断続的に処理
してもよく、装置などにもとくに限定はなく、たとえば
熱風乾燥機などの加熱炉を使用して加熱炉中に静置した
り、加熱炉中をゆっくりと移動させながら処理すればよ
いが、60〜100℃で1〜24時間処理するのが好ましい。
該処理温度が40℃未満であると、永久歪を小さくする効
果がほとんどなく好ましくなく、120℃をこえると、永
久歪を小さくする効果がほとんどない上、成形品が変形
したり、外観が悪化したりするばあいがあり、好ましく
ない。また、該処理時間が20分未満であると、永久歪を
小さくする効果がほとんどなく好ましくない。
The heat treatment of the foamed molded product may be continuous treatment as long as it is heat treated at 40 to 120 ° C. for 20 minutes or more, or may be intermittent treatment, and there is no particular limitation on the device, for example, hot air drying. The treatment may be carried out by leaving it in the heating furnace by using a heating furnace such as a machine or by moving it slowly in the heating furnace, but it is preferable to perform the treatment at 60 to 100 ° C. for 1 to 24 hours.
If the treatment temperature is lower than 40 ° C, there is almost no effect of reducing the permanent set, which is not preferable, and if it exceeds 120 ° C, there is almost no effect of reducing the permanent set, and the molded product is deformed or the appearance is deteriorated. There is a possibility of doing so, which is not preferable. Further, if the treatment time is less than 20 minutes, there is almost no effect of reducing the permanent set, which is not preferable.

このようにしてえられる発泡成形品は発泡倍率1.2〜3.5
倍、圧縮永久歪が25〜45%程度で、緻密で均一な独立発
泡セルを有しており、シール性、クッション性、ゴム様
弾性、遮音性、断熱性に優れたものである。また、とく
に押出発泡成形により成形され、加熱処理をしてえられ
る成形品は、表面平滑性も極めて良好であり、外観の良
好なことが必要な製品分野にとくに好適である。
The foamed molded product thus obtained has a foaming ratio of 1.2 to 3.5.
Twice the compression set is about 25-45%, and it has dense and uniform closed cells, and is excellent in sealing, cushioning, rubber-like elasticity, sound insulation and heat insulation. Further, a molded product obtained by extrusion foam molding and obtained by heat treatment has particularly excellent surface smoothness and is particularly suitable for a product field requiring a good appearance.

なお、本発明にいう圧縮永久歪は第2図に示すスペーサ
ー(3)を有する装置(4)を用いて、JIS K 6301の圧縮永久
歪の測定法と同様な方法で圧縮率53%、圧縮条件70℃×
22時間で測定した値である。この圧縮永久歪の測定値
は、成形品の形状によってかなり異なることがあり、上
記25〜45%の値も形状によっては、たとえば20〜50%に
なることもある。
The compression set referred to in the present invention was measured by using the apparatus (4) having the spacer (3) shown in FIG. Condition 70 ℃ ×
It is a value measured in 22 hours. The measured value of the compression set may vary considerably depending on the shape of the molded product, and the value of 25 to 45% may be, for example, 20 to 50% depending on the shape.

このようにしてえられる永久歪の小さい軟質塩化ビニル
系樹脂組成物発泡成形品は、たとえばモール類、グラス
ランチャンネル類、ウェザーストリップ類、トリム類、
各種のクッション部材、各種のシール部材などの自動車
用部品、滑り止め用、家具類の縁取用、シール用などの
建材部品、遮音用、防振用、断熱用、保護用、シール
用、クッション用などの目的で、シート状、チューブ状
または各種の異形状の物品として、軟質塩化ビニル系樹
脂、ポリウレタン、EPDMなどの成形品が使用されている
分野などに好適に利用されうる。
The soft vinyl chloride-based resin composition foam-molded article having a small permanent set thus obtained is, for example, moldings, glass run channels, weather strips, trims,
Various cushioning members, automotive parts such as various sealing members, slip prevention, edging of furniture, building material parts such as sealing, sound insulation, vibration isolation, heat insulation, protection, sealing, cushioning For such a purpose, it can be suitably used as a sheet-shaped, tube-shaped or various shaped article in a field where molded articles such as soft vinyl chloride resin, polyurethane and EPDM are used.

以下に本発明の永久歪を小さくした軟質塩化ビニル系樹
脂組成物発泡成形品の製法を実施例により更に詳しく説
明するが、本発明はこれらに限定されるものではない。
Hereinafter, the method for producing a foamed molded product of a soft vinyl chloride resin composition having a reduced permanent set according to the present invention will be described in more detail with reference to Examples, but the present invention is not limited thereto.

実施例1〜9および比較例1〜3 第1表に示す平均重合度を有する塩化ビニル系樹脂100
部に、第1表に示す比粘度およびガラス転移温度を有す
るメタクリル酸メチル系共重合体を第1表に示す量、ジ
オクチルフタレート(以下、DOPという)を第1表に示
す量、Ba-Zn系安定剤3部、炭酸カルシウム20部、発泡
剤を第1表に示す量添加し、スーパーミキサーを用いて
ドライアップさせた。えられたパウダーコンパウンドを
140℃で10分間混練し、厚さ約3mmの素練りシートを作
製したのち、約3mm四方に切断してペレット化し、押出
発泡成形を行なった。
Examples 1 to 9 and Comparative Examples 1 to 3 Vinyl chloride resin 100 having an average degree of polymerization shown in Table 1
In the parts, a methyl methacrylate copolymer having a specific viscosity and a glass transition temperature shown in Table 1 is shown in Table 1, dioctyl phthalate (hereinafter referred to as DOP) is shown in Table 1, Ba-Zn. 3 parts of a system stabilizer, 20 parts of calcium carbonate and a foaming agent were added in amounts shown in Table 1 and dried up using a super mixer. The obtained powder compound
After kneading at 140 ° C. for 10 minutes to prepare a masticated sheet having a thickness of about 3 mm, the masticated sheet was cut into about 3 mm square and pelletized, and extrusion foam molding was performed.

押出発泡成形はL/D=22、圧縮比=3.0のフルフライトス
クリューを使用し、50mm単軸押出機にて、シリンダー温
度をホッパー側よりC1=155℃、C2=170℃、C3=170
℃、アダプター=150℃、ダイ=140℃に設定し、スクリ
ュー回転数40rpmで行ない、第1図に示す形の異形押出
成形用金型(1)を用いて、自動車用シール部材(2)を押出
した。成形品は、空冷により自由発泡させたのち、第1
表の条件で加熱処理を行ない、下記方法による比重測定
および外観評価に供したのち、その成形品を第2図に示
すスペーサー(3)を有する装置(4)を用いて、JIS K 6301
の圧縮永久歪の測定法と同様の方法で永久歪を測定し
た。なお、圧縮率は53%、圧縮条件は70℃で22時間とし
た。結果を第1表に示す。
Extrusion foaming molding using L / D = 22, full flight screw of a compression ratio = 3.0, at 50mm single-screw extruder, C 1 = 155 ° C. from a hopper side cylinder temperature, C 2 = 170 ℃, C 3 = 170
C., adapter = 150.degree. C., die = 140.degree. C., screw speed 40 rpm, and using the extrusion die (1) of the shape shown in FIG. Extruded. The molded product is allowed to freely foam by air cooling and then
Heat treatment was performed under the conditions shown in the table, and the specific gravity was measured and the appearance was evaluated by the following methods. The molded product was then subjected to JIS K 6301 using an apparatus (4) having a spacer (3) shown in FIG.
The permanent set was measured by the same method as the method for measuring the compression set of. The compression rate was 53%, and the compression condition was 70 ° C. for 22 hours. The results are shown in Table 1.

(成形品の比重および発泡倍率) JIS K 7112の水中置換法で比重を測定し、非発泡成形品
の比重を発泡成形品の比重で除して発泡倍率を求めた。
(Specific gravity and expansion ratio of molded product) The specific gravity was measured by the water substitution method of JIS K 7112, and the specific gravity of the non-foamed molded product was divided by the specific gravity of the foamed molded product to obtain the expansion ratio.

(成形品の外観) 目視観察によって行ない、表面平滑性およびセル状態に
ついて下記基準に基づき評価した。なお、セル状態は成
形品をカッターナイフで切断し、その切断面を観察し
た。
(Appearance of molded product) Visual observation was carried out and surface smoothness and cell condition were evaluated based on the following criteria. In addition, in the cell state, the molded product was cut with a cutter knife and the cut surface was observed.

表面平滑性 ○:平滑 △:凹凸が目立つ ×:凹凸が著しい セル状態 ○:均一な独立セル △:部分的にセルの連通がある ×:セルの連通が著しく、空洞がある 第1表の結果から、メタクリル酸メチル系共重合体の比
粘度が1.4〜2.1のものを使用すると、加熱処理前の外観
がわるいが、メタクリル酸メチル系共重合体の比粘度が
2.9以上のものを使用すると、加熱処理前の成形品の外
観が非常に良好で、かつ、発泡倍率も比較例に比べて高
くなっていることがわかる。さらに、加熱処理前の圧縮
永久歪は、実施例のものでも50〜65%と大きいが、70℃
で24時間の加熱処理を行なうこによって、28〜43%とEP
DMと同等の値にまで低くしうることがわかる。
Surface smoothness ○: Smooth Δ: Concavo-convex is conspicuous ×: Concavo-convex is remarkable Cell state ○: Uniform independent cell △: Cell communication is partially ×: Cell communication is remarkable, and void is present From the results shown in Table 1, when a methyl methacrylate copolymer having a specific viscosity of 1.4 to 2.1 is used, the appearance before heat treatment is poor, but the methyl methacrylate copolymer has a specific viscosity of
It can be seen that the use of 2.9 or more results in a very good appearance of the molded product before heat treatment, and also has a higher expansion ratio than the comparative example. Furthermore, the compression set before heat treatment is as large as 50 to 65% even in the example, but 70 ° C.
By heat treatment for 24 hours at 28-43% and EP
It can be seen that it can be lowered to a value equivalent to DM.

実施例10〜16および比較例4〜6 第2表に示す組成物を用いて実施例1と同様にして評価
した。結果を第2表に示す。
Examples 10 to 16 and Comparative Examples 4 to 6 The compositions shown in Table 2 were used and evaluated in the same manner as in Example 1. The results are shown in Table 2.

第2表の結果から、加熱処理温度が低いと、圧縮永久歪
を小さくできず、逆に130℃と高過ぎると、圧縮永久歪
を小さくできないばかりでなく、成形品の外観が悪化す
ることがわかる。さらに、加熱処理時間が0.2時間と短
か過ぎると、圧縮永久歪を小さくできないことがわか
る。一方、加熱処理時間を0.5時間以上にして加熱処理
温度を70〜100℃にすると、圧縮永久歪を大幅に小さく
しうることがわかる。
From the results shown in Table 2, the compression set cannot be reduced when the heat treatment temperature is low, and conversely, when it is too high at 130 ° C, not only the compression set cannot be reduced, but also the appearance of the molded product is deteriorated. Recognize. Furthermore, it can be seen that the compression set cannot be reduced if the heat treatment time is as short as 0.2 hours. On the other hand, when the heat treatment time is 0.5 hours or more and the heat treatment temperature is 70 to 100 ° C., it is understood that the compression set can be significantly reduced.

[発明の効果] 本発明の方法による軟質塩化ビニル系発泡成形品は、1.
2倍以上の発泡倍率を有しながら、セル状態が均一で独
立性に優れており、しかも永久歪が小さいという特徴を
有するものである。
[Advantages of the Invention] The flexible vinyl chloride foam-molded article produced by the method of the present invention is
While having a foaming ratio of 2 times or more, it is characterized by a uniform cell state, excellent independence, and a small permanent set.

それゆえ、遮音性、防振性、断熱性、保護性、シール
性、クッション性などに優れた軟質塩化ビニル系発泡成
形品をうることができる。さらに、押出成形法によっ
て、安価に、簡単に、しかも外観の優れた成形品を製造
することが可能で、従来、EPDM、ポリウレタンゴムの発
泡体しか使用できなかった分野においても充分使用する
ことができる。
Therefore, it is possible to obtain a soft vinyl chloride-based foam molded article which is excellent in sound insulation, vibration isolation, heat insulation, protection, sealing, cushioning and the like. Furthermore, the extrusion molding method makes it possible to inexpensively and easily produce a molded product having an excellent appearance, and it can be sufficiently used even in the field where only foams of EPDM and polyurethane rubber can be conventionally used. it can.

【図面の簡単な説明】[Brief description of drawings]

第1図は、軟質塩化ビニル系樹脂組成物発泡成形品の圧
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
出成形用金型の先端断面形状を示す説明図、第2図は、
第1図に示す金型を用いて製作した試験片を用いて圧縮
永久歪を測定する方法を示す説明図である。
FIG. 1 is an explanatory view showing the tip cross-sectional shape of a die for extrusion molding of a seal member for automobile parts for evaluating compression set of a soft vinyl chloride resin composition foam molded article, and FIG.
It is explanatory drawing which shows the method of measuring a compression set using the test piece manufactured using the metal mold | die shown in FIG.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】塩化ビニル系樹脂100重量部に対して、メ
タクリル酸メチルを主成分とする共重合体0.4gを含む1
00mlのベンゼン溶液の30℃で測定した比粘度が2.5以上
のメタクリル酸メチル系共重合体1〜30重量部、可塑剤
20〜200重量部および発泡剤0.5〜10重量部を含む発泡用
軟質塩化ビニル系樹脂組成物を発泡成形してえられた成
形品を40〜120℃の温度で20分間以上加熱処理すること
を特徴とする発泡倍率1.2〜3.5倍で永久歪の小さい軟質
塩化ビニル系発泡成形品の製法。
1. A polymer containing 0.4 g of a copolymer containing methyl methacrylate as a main component per 100 parts by weight of a vinyl chloride resin.
1 to 30 parts by weight of methyl methacrylate copolymer having a specific viscosity of 2.5 or more in 00 ml of benzene solution measured at 30 ° C., a plasticizer
A molded product obtained by foam molding a soft vinyl chloride resin composition for foaming containing 20 to 200 parts by weight and 0.5 to 10 parts by weight of a foaming agent is subjected to heat treatment at a temperature of 40 to 120 ° C for 20 minutes or more. A method for producing soft vinyl chloride foamed molded products with a characteristic expansion ratio of 1.2 to 3.5 times and a small permanent set.
【請求項2】40〜120℃の温度で20分間以上の加熱処理
が連続的または断続的に行なわれる特許請求の範囲第1
項記載の製法。
2. The method according to claim 1, wherein the heat treatment at a temperature of 40 to 120 ° C. for 20 minutes or more is carried out continuously or intermittently.
The manufacturing method described in paragraph.
JP61214689A 1986-09-11 1986-09-11 Manufacturing method of soft vinyl chloride foam moldings with small permanent set Expired - Fee Related JPH0657758B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP61214689A JPH0657758B2 (en) 1986-09-11 1986-09-11 Manufacturing method of soft vinyl chloride foam moldings with small permanent set
JP5233221A JPH0774286B2 (en) 1986-09-11 1993-09-20 Flexible vinyl chloride foamed molded product with small permanent set

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61214689A JPH0657758B2 (en) 1986-09-11 1986-09-11 Manufacturing method of soft vinyl chloride foam moldings with small permanent set

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP5233221A Division JPH0774286B2 (en) 1986-09-11 1993-09-20 Flexible vinyl chloride foamed molded product with small permanent set

Publications (2)

Publication Number Publication Date
JPS6369838A JPS6369838A (en) 1988-03-29
JPH0657758B2 true JPH0657758B2 (en) 1994-08-03

Family

ID=16659962

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61214689A Expired - Fee Related JPH0657758B2 (en) 1986-09-11 1986-09-11 Manufacturing method of soft vinyl chloride foam moldings with small permanent set

Country Status (1)

Country Link
JP (1) JPH0657758B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6028299A (en) * 1983-07-27 1985-02-13 ソニー株式会社 Clinch state discriminator of lead wire of electronic part

Also Published As

Publication number Publication date
JPS6369838A (en) 1988-03-29

Similar Documents

Publication Publication Date Title
CN1802408A (en) Method for the production of expanding thermoplastic elastomers
CN105440243B (en) Urethane composition and preparation method thereof for vehicle dormer window cushion pad
US4956396A (en) Process for preparing rigid polyvinyl chloride stractured foams having superior surface characteristics
JPH0657758B2 (en) Manufacturing method of soft vinyl chloride foam moldings with small permanent set
JPH06192458A (en) Flexible vinyl chloride foamed molded product with small permanent set
JPH0657759B2 (en) Manufacturing method of soft vinyl chloride foam moldings with small permanent set
JPH07107106B2 (en) Flexible vinyl chloride foamed molded product with small permanent set
JPH0657760B2 (en) Pellet-shaped flexible vinyl chloride resin composition used for extrusion molding
JPS63125536A (en) Foamed flexible vinyl chloride molding and its production
JPS63139927A (en) Extrusion-foamable flexible vinyl chloride resin composition
JP2002194126A (en) Vinyl chloride resin composition for blow molding, blow molded article and molded laminate
JPS55149328A (en) Preparation of foamed vinyl chloride resin molded article
JPS63139928A (en) Flexible vinyl chloride resin foam and its production
JPS58189238A (en) Expanded vinyl cyloride resin composition
JP2805681B2 (en) Thermoplastic elastomer composition
JPH08120108A (en) Expandable vinyl chloride resin composition
JPH0482034B2 (en)
JPH11255990A (en) Thermoplastic elastomer resin composition, its extruded product and window frame
EP0189286A2 (en) Process for making foamed, sulfur-cured polymer blend compositions
JPS5618627A (en) Production of vinyl chloride-based synthetic resin foam
JPH11270247A (en) Window frame
JPS61276835A (en) Production of crosslinked soft polyvinyl chloride foam
KR20000018117A (en) Producing method of bubbling soft pvc
JP2000129026A (en) Foam sheet and molded article comprising modified polypropylene resin composition
JPS6028299B2 (en) Method for manufacturing soft vinyl chloride resin foam molded product

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees