JPH07107106B2 - Flexible vinyl chloride foamed molded product with small permanent set - Google Patents

Flexible vinyl chloride foamed molded product with small permanent set

Info

Publication number
JPH07107106B2
JPH07107106B2 JP5233233A JP23323393A JPH07107106B2 JP H07107106 B2 JPH07107106 B2 JP H07107106B2 JP 5233233 A JP5233233 A JP 5233233A JP 23323393 A JP23323393 A JP 23323393A JP H07107106 B2 JPH07107106 B2 JP H07107106B2
Authority
JP
Japan
Prior art keywords
vinyl chloride
molded product
parts
chloride resin
foamed molded
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
JP5233233A
Other languages
Japanese (ja)
Other versions
JPH06192457A (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
Priority claimed from JP61214690A external-priority patent/JPH0657759B2/en
Application filed by Kaneka Corp filed Critical Kaneka Corp
Priority to JP5233233A priority Critical patent/JPH07107106B2/en
Publication of JPH06192457A publication Critical patent/JPH06192457A/en
Publication of JPH07107106B2 publication Critical patent/JPH07107106B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、成形品の発泡倍率が
1.2〜 2.5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に関す
る。
BACKGROUND OF THE INVENTION The present invention has a foaming ratio of a molded product.
The present invention relates to a foam-molded article made of a specific soft vinyl chloride resin composition having a ratio of 1.2 to 2.5 times and a small permanent set.

【0002】[0002]

【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。
2. Description of the Related 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 its sound insulation, heat insulation and sealing properties. Although a foamed molded product from is manufactured and used, it is possible to obtain a soft vinyl chloride foamed molded product that has dense and uniform independent foam cells, expansion ratio of 1.2 times or more, and small permanent set. Not used, and used only to a limited extent.

【0003】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 foamed molded article, there are an extrusion foaming molding method, an injection molding method, a calender molding method, and the like, and a method of manufacturing using an evaporative foaming agent and a decomposition type foaming agent. There is a manufacturing method using.

【0004】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、この押出発泡成形品の分
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 production method using a decomposition type foaming agent by the extrusion foam molding method has the advantages that it can be diverted by slightly modifying the conventionally used extruder and that the process is simple. It is widely used in the production of low-foam to medium-foam molded products. In particular, in the field of extrusion foam molded products, in addition to permanent set, expansion ratio, and uniformity of foam cells, a molded product having a stable extrusion shape, a smooth surface, and a good appearance is demanded. , Such foam-molded products have not been obtained.

【0005】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
られていない。
The addition of a processability improver is a generally adopted method for solving the problems such as the expansion ratio of foamed molded products, the uniformity of foam cells, and the moldability in extrusion molding. It is well known that the 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.

【0006】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
泡成形品はえられていない。
That is, in a general extrusion foam molding method, even if a commonly used copolymer containing methyl methacrylate as a main component and having a specific viscosity of 1 to 2 is added, it is dense and uniform. It has an independent foam cell and a foaming ratio of 1.2.
It is not possible to obtain a foamed molded product having a surface smoothness of more than double. Further, even in the injection molding method or the like, the addition of the processability improver having the specific viscosity of 1 to 2 causes the expansion ratio to be increased.
No foamed molded product with a density of 1.2 or more and dense and uniform closed cells has been obtained.

【0007】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点は、より顕著に
現われる。このため、この部分架橋のアクリロニトリル
−ブタジエンゴムの添加のみでは、圧縮永久歪が50%以
下で、かつ発泡倍率 1.2以上で緻密で均一な発泡セルを
有する発泡成形体をうることはきわめて困難である。
On the other hand, as disclosed in JP-A-61-66732, a decomposable foaming agent is added to a soft vinyl chloride resin composition containing a partially crosslinked acrylonitrile-butadiene rubber for the purpose of reducing permanent set. When extrusion foaming is carried out by adding, the permanent strain is reduced, but the problem that the expansion ratio is difficult to increase and uniform foam cells cannot be obtained becomes more prominent. Therefore, it is extremely difficult to obtain a foamed molded product having a compression set of 50% or less and a dense and uniform foam cell with a foaming ratio of 1.2 or more, only by adding the partially crosslinked acrylonitrile-butadiene rubber. .

【0008】[0008]

【発明が解決しようとする課題】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
えようとする際に、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。
DISCLOSURE OF THE INVENTION The present invention, when trying to obtain a soft vinyl chloride resin composition foam-molded article by various foam-molding methods, according to the conventional technique, the foamed state of the foam-molded article is dense and uniform. The state of independent foam cells and the expansion ratio
This is done to solve the problem that a foamed molded product having a ratio of 1.2 times or more and a reduced permanent set cannot be obtained, and that it is used only in a limited range.

【0009】[0009]

【課題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、メチルエ
チルケトン(以下、MEKという)に5〜90%(重量
%、以下同様)溶解するアクリロニトリル―ブタジエン
ゴム(以下、NBRという)5〜150部、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100
ml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共重合体1〜60部および可
塑剤20〜200部を含む軟質塩化ビニル系樹脂組成物
からなる発泡倍率1.2〜2.5倍で永久歪15〜40
%の軟質塩化ビニル系発泡成形品に関する。
According to the present invention, 100 parts (parts by weight, hereinafter the same) of vinyl chloride resin dissolves in methyl ethyl ketone (hereinafter, referred to as MEK) by 5 to 90% (% by weight, the same below). 100 including acrylonitrile-butadiene rubber (hereinafter referred to as NBR) 5 to 150 parts and a copolymer containing methyl methacrylate as a main component 0.4 g
2.5 ml specific viscosity of benzene solution measured at 30 ° C is 2.5
Permanent set 15-40 at a foaming ratio of 1.2-2.5, which is made of a soft vinyl chloride resin composition containing 1 to 60 parts of the above methyl methacrylate copolymer and 20 to 200 parts of a plasticizer.
% Soft vinyl chloride foam molded article.

【0010】[0010]

【作用および実施例】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―を単独重合させた塩化ビニ
ル樹脂または85%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。
[Functions and Examples] 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 copolymer containing 85% or more vinyl chloride. It may be a partially cross-linked vinyl chloride resin containing a component, and any conventionally known vinyl chloride resin may be used as long as it complies with the above regulations.

【0011】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 the like.
Butyl (meth) acrylate, (meth) acrylic acid-2-ethylhexyl and other (meth) acrylic acid esters, butyl maleate, octyl maleate and other maleic esters, butyl fumarate, fumaric octyl and other fumarates Examples thereof include acid esters and these acids, but are not limited thereto. Two or more of these components other than vinyl chloride may be used in combination.

【0012】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, polyfunctional compounds such as diallyl phthalate, diallyl maleate, polyethylene glycol di (meth) acrylate and 1,2-polybutadiene as a crosslinking agent are used. Examples thereof include resins obtained by copolymerization using, but are not limited to these.

【0013】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 kinds of these vinyl chloride resins may be used in combination, and the ratio of the combination may be freely selected according to the purpose.

【0014】塩化ビニル系樹脂の平均重合度は 600〜45
00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 vinyl chloride resin has an average degree of polymerization of 600 to 45.
It is preferably 00, particularly preferably 1000 to 3200. If 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 product 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.

【0015】本発明に使用するNBRとは、MEKに5
〜90%(25℃)、好ましくは10〜60%溶解する部分架橋
NBRのことである。MEKに5〜90%(25℃)溶解す
る部分架橋NBRを用いると、発泡成形品の圧縮永久歪
を小さくし、応力を加えたのちの復元力を向上させるこ
とができるのみならず、発泡成形する際、溶融粘度の温
度依存性を小さくしうるため、発泡成形時の温度巾を広
げることができる。
The NBR used in the present invention is 5 in MEK.
It is a partially crosslinked NBR that dissolves at 90% (25 ° C), preferably at 10-60%. Use of partially crosslinked NBR that dissolves in MEK at 5 to 90% (25 ° C) not only reduces the compression set of foamed molded products and improves the restoring force after stress is applied, but also foamed molding. At this time, the temperature dependence of the melt viscosity can be reduced, so that the temperature range during foam molding can be widened.

【0016】前記NBRがMEKに90%をこえて溶解す
るばあいには、圧縮永久歪を小さくする効果および発泡
成形時の温度依存性を小さくする効果が不足し、好まし
くない。逆に、MEKに5%未満しか溶解しないばあい
には、成形性が低下し、好ましくない。
If the NBR is dissolved in MEK in an amount of more than 90%, the effect of reducing the compression set and the effect of reducing the temperature dependency during foam molding are insufficient, which is not preferable. On the other hand, if less than 5% is dissolved in MEK, the moldability is lowered, which is not preferable.

【0017】なお、MEKに溶解するとは、25℃の温度
でMEKで48時間抽出し、 100メッシュのフィルタ―を
通過することを意味する。
Dissolving in MEK means extracting with MEK at a temperature of 25 ° C. for 48 hours and passing through a 100-mesh filter.

【0018】本発明に用いるNBRは、塩化ビニル系樹
脂 100部に対して5〜 150部、好ましくは10〜 120部使
用される。該使用量が5部未満では、圧縮永久歪を小さ
くする効果が充分えられなくなり好ましくない。逆に、
150部をこえると、ペレット製造時の混練性、発泡成形
時の成形性がわるくなり、さらに、耐熱老化性、耐オゾ
ン性、耐候性などがわるくなり好ましくない。
The NBR used in the present invention is used in an amount of 5 to 150 parts, preferably 10 to 120 parts, per 100 parts of the vinyl chloride resin. If the amount used is less than 5 parts, the effect of reducing the compression set is not sufficiently obtained, which is not preferable. vice versa,
If it exceeds 150 parts, the kneading property at the time of pellet production, the moldability at the time of foam molding become poor, and further the heat aging resistance, ozone resistance, weather resistance and the like become poor, which is not preferable.

【0019】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 contains methyl methacrylate as a main component, that is, contains 50 to 95% of methyl methacrylate, and an acrylic acid ester and / or a methacrylic acid ester (methyl methacrylate). And (or) a small amount of a cross-linking agent or a graft copolymer.

【0020】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 30 times that of 100 ml of a benzene solution containing 0.4 g of the copolymer.
Specific viscosity measured at ℃ is 2.5 or more, preferably 2.5 to 6.0
And a glass transition temperature of 85 ° C. or lower. The specific viscosity is
When it is less than 2.5, the uniformity and independence of the cells of the foamed molded product, the surface smoothness of the extrusion molded product, and the like are not improved, and the expansion ratio is not increased, which is not preferable. Further, in order to improve the kneading property at the time of producing the pellet compound, the glass transition temperature is preferably 85 ° C. or lower.

【0021】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1〜60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60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 copolymer used in the present invention is used in an amount of 1 to 60 parts per 100 parts of vinyl chloride resin. 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 60 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.

【0022】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 product flexibility and rubber feel, and specific examples thereof include dibutyl phthalate, dioctyl phthalate, diisodecyl phthalate, and the like.
Alkyl esters of aromatic polybasic acids such as diisononyl phthalate, diundecyl phthalate, trioctyl trimellitate, triisooctyl trimellitate, dibutyl adipate, dioctyl adipate, diisononyl adipate, dibutyl azelate, dioctyl azelate, diisononyl azelate Alkyl esters of aliphatic polybasic acids such as, phosphoric acid alkyl esters such as tricresyl phosphate, and further polyester plasticizers,
Examples of the commonly used plasticizers include epoxy plasticizers and chlorinated paraffins. These may be used alone or in combination of two or more.

【0023】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 based on 100 parts of vinyl chloride resin
20 to 200 parts, preferably 30 to 160 parts are used. If the amount used exceeds 200 parts, the heat distortion resistance of the molded product and the independence of the cells are deteriorated, which is not preferable. , Not preferable.

【0024】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'-dinitrosoterephthalamide, N, N'-dinitrosopentamethylenetetramine, p-toluenesulfonylhydrazide, benzene-1,3-disulfonylhydrazide, diphenylsulfone-3,3'-disulfonylhydrazide, p-toluene Examples thereof include sulfonyl semicarbazide. These may be used alone or in combination of two or more kinds as appropriate.

【0025】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部
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 based on 100 parts of vinyl chloride resin
0.5-10 parts, preferably 1.5-5 parts are used. 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 parts, it is not preferable because over-foaming results in cell breakage and communication, and the uniformity and independence of the cells deteriorate.

【0026】本発明の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、ゴム類(部分架橋NBRを除く)、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 the foamed molded article of the present invention, if necessary, stabilizers, lubricants, fillers, ultraviolet absorbers, pigments, rubbers (excluding partially crosslinked NBR), polyurethane resins, polyester resins, etc. Resin, ethylene-vinyl acetate copolymer, thermoplastic resin such as chlorinated polyethylene may be blended and used, and further, a kicking agent, a decomposition inhibitor, a foaming aid such as a cell regulator may be used. Well, the kind and the addition amount may be appropriately selected according to the purpose.

【0027】本発明の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。
In producing the soft vinyl chloride foamed molded article of the present invention, the components are blended and pelletized by using, for example, a step of producing a general soft vinyl chloride resin composition, and then the pellets are foamed. It may be molded, and then the molded product may be heat-treated.

【0028】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てもよく、ドラ
イアップさせる途中で投入してもよい。
That is, at the time of blending, a conventionally known blender such as a Henschel mixer, a super mixer or a ribbon blender is used, and after adding components such as a vinyl chloride resin, the plasticizer is added all at once, intermittently or continuously. The temperature is raised to 80-150 ° C to dry up the plasticizer to 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.

【0029】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、 1
00〜 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 fed to a pressure kneader, a cokneader, a mixing roll, various extruders, etc.
Kneading is performed at a temperature of 00 to 200 ° C to produce a pellet compound of a soft vinyl chloride resin composition.

【0030】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 molding method which has been generally used in the past, such as an extrusion molding method, an injection molding method or a calender molding method can be used.

【0031】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。
In the case of molding by the extrusion foam molding method, extrusion molding using various single-screw or twin-screw extruders equipped with dies having various shapes according to the purpose of the molded product of the pellet compound. A soft vinyl chloride foamed molded product is manufactured by the molding method. During extrusion foam molding, it may be coextruded with metal, soft PVC, hard PVC, or the like.

【0032】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
It is carried out 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 it is preferable to carry out molding while maintaining the temperature difference at 5 ° C. or more.

【0033】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、スクリューの圧縮
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 screw compression ratio is preferably 1.0 to 5.0, and particularly 1.5 to 5.0.
3.5 is preferable.

【0034】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〜 2.5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, at a foaming ratio of 1.2 to 2.5 obtained by extrusion molding, injection molding, calender molding, etc.,
In addition, 40 foam molded products with dense and uniform independent foam cells
Heat treatment at 120 ° C for 20 minutes or more significantly improves the permanent set. Up to now, there is no known method for significantly reducing the permanent set by heat treatment.

【0035】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 is carried out at 40 to 120 ° C. for 20 hours.
As long as it is heat-treated for more than 1 minute, it may be treated continuously,
It may be processed intermittently, and there is no particular limitation on the device, and it may be left standing in a heating furnace such as a hot air dryer,
The treatment may be carried out while slowly moving in the heating furnace, but it is preferable to carry out 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.

【0036】このようにしてえられる発泡成形品は発泡
倍率1.2〜2.5倍、圧縮永久歪が15〜40%で
緻密で均一な独立発泡セルを有しており、ゴム用弾性、
シール性、クッション性、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 2.5 and a compression set of 15 to 40 % .
It has dense and uniform independent foam cells, and has elasticity for rubber,
It has excellent sealing properties, cushioning properties, sound insulation properties, and heat insulation properties. 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.

【0037】なお、本発明にいう圧縮永久歪は図2に示
すスペーサー3を有する装置4を用いてJIS K 63
01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。
The compression set referred to in the present invention is measured according to JIS K 63 using the device 4 having the spacer 3 shown in FIG.
The value was measured by the same method as the method for measuring the compression set of 01 at a compression rate of 53% and a compression condition of 70 ° C for 22 hours.

【0038】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15〜40%の値も
形状によっては、たとえば10〜45%になることもある。
The measured value of the compression set may vary considerably depending on the shape of the molded product, and the value of 15 to 40% may be, for example, 10 to 45% depending on the shape.

【0039】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 foamed molded product of the soft vinyl chloride resin composition having a small permanent strain thus obtained is, for example, moldings, glass run channels, weather strips, trims, various cushion members, various sealing members, etc. Automotive parts, non-slip, furniture edging,
Soft vinyl chloride resin as a sheet-shaped, tube-shaped or various shaped article for the purpose of building materials such as seals, sound insulation, vibration isolation, heat insulation, protection, sealing, cushioning, etc. It can be preferably used in fields where molded articles such as polyurethane and EPDM are used.

【0040】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。
The foamed molded product of the soft vinyl chloride resin composition having a reduced permanent set according to the present invention will be described in more detail below with reference to Examples, but the present invention is not limited thereto.

【0041】実施例1〜10および比較例1〜3 表1に示す平均重合度を有する塩化ビニル樹脂 100部
に、表1に示すMEKに対する溶解性を有する部分架橋
NBR(アクリロニトリル成分33%)を表1に示す量、
表1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表1に示す量、ジオクチルフ
タレート(以下、DOPという)を表1に示す量、Ba
−Zn系安定剤3部、炭酸カルシウム20部、発泡剤を表
1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 10 and Comparative Examples 1 to 3 To 100 parts of vinyl chloride resin having an average degree of polymerization shown in Table 1, partially crosslinked NBR having solubility for MEK shown in Table 1 (33% of acrylonitrile component) was added. The amount shown in Table 1,
The amount of the methyl methacrylate copolymer having the specific viscosity and the glass transition temperature shown in Table 1 shown in Table 1, the amount of dioctyl phthalate (hereinafter referred to as DOP) shown in Table 1, Ba,
A Zn-based stabilizer (3 parts), calcium carbonate (20 parts) and a foaming agent were added in the amounts shown in Table 1 and dried up using a super mixer. The obtained powder compound at 140 ℃
After kneading 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.

【0042】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℃、C
2 =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、
図1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、表1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
成形品を図2に示すスペーサー3を有する装置4を用い
て、JIS K6301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(予め70℃で予熱しておいた図2に
示す装置4に、厚さ(図2の上下圧縮板間に相当)を測
った成形品2を圧縮率が53%になるように上部圧縮板で
スペーサー3まで押し、圧縮板をボルトで固定する。成
形品をセット後、直ちに70℃の恒温槽に入れる。22時間
後、成形品2をこの装置から取出し室温で放冷し、30分
後に厚さを測定し、次式により圧縮永久歪を求める。
In extrusion foam molding, L / D = 22, compression ratio = 3.0
Cylinder temperature from the hopper side to C 1 = 155 ° C, C
2 = 170 ° C, C 3 = 170 ° C, adapter = 150 ° C, die = 140 ° C, screw rotation speed 40 rpm,
An automobile seal member 2 was extruded using a profile extrusion mold 1 having the shape shown in FIG. The molded product was subjected to free foaming by air cooling and then subjected to a heat treatment under the conditions shown in Table 1, subjected to specific gravity measurement and appearance evaluation by the following methods, and then the molded product was subjected to an apparatus 4 having a spacer 3 shown in FIG. Then, the permanent set was measured by the same method as the method for measuring the compression set of JIS K6301 (in the apparatus 4 shown in FIG. 2 preheated at 70 ° C., the thickness (between the upper and lower compression plates in FIG. 2) was measured. The molded product 2 which has been measured is pressed to the spacer 3 with the upper compression plate so that the compression rate becomes 53%, and the compression plate is fixed with bolts.After setting the molded product, immediately put it in a constant temperature bath at 70 ° C. After 22 hours, the molded product 2 is taken out of the apparatus and allowed to cool at room temperature, and after 30 minutes, the thickness is measured, and the compression set is determined by the following formula.

【0043】[0043]

【数1】 [Equation 1]

【0044】(式中、t0 は成形品2のもとの厚さ(m
m)、t1 は装置4から取出した成形品2を30分間放冷
したのちの厚さ(mm)、t2 はスペーサー3の長さ(m
m)))。結果を表1に示す。
(Where t 0 is the original thickness of the molded product 2 (m
m), t 1 is the thickness (mm) after the molded product 2 taken out from the apparatus 4 is allowed to cool for 30 minutes, and t 2 is the length of the spacer 3 (m
m))). The results are shown in Table 1.

【0045】(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) JIS
The specific gravity was measured by the underwater substitution method of 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.

【0046】(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―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 to evaluate surface smoothness and cell condition based on the following criteria. For the cell state, the molded product was cut with a cutter knife and the cut surface was observed.

【0047】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Surface smoothness ○: Smoothness Δ: Conspicuous irregularities ×: Conspicuous irregularities in cell state ○: Uniform independent cells Δ: Partial cell communication ×: Cell communication is significant, voids

【0048】[0048]

【表1】 [Table 1]

【0049】表1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37〜62%と大
きいが、70℃で24時間の加熱処理を行なうことによっ
て、18〜40%とEPDMと同等の値にまで低くしうるこ
とがわかる。
From the results shown in Table 1, when a methyl methacrylate-based copolymer having a specific viscosity of 1.4 to 2.1 is used, the appearance before heat treatment is poor, but the methyl methacrylate-based copolymer has a specific viscosity of 2.9. It can be seen that when the above-mentioned materials are used, the appearance of the molded product before the heat treatment is very good and the expansion ratio is higher than that of the comparative example. Further, the compression set before the heat treatment is as large as 37 to 62% even in the example, but by performing the heat treatment at 70 ° C for 24 hours, it is lowered to 18 to 40%, which is a value equivalent to that of EPDM. I understand that it is possible.

【0050】実施例11〜17および比較例4〜6 表2に示す組成物を用いて実施例1と同様にして評価し
た。結果を表2に示す。
Examples 11 to 17 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.

【0051】[0051]

【表2】 [Table 2]

【0052】表2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, when the heat treatment temperature is low,
If the compression set cannot be reduced and conversely it is too high at 130 ℃,
It can be seen that not only the compression set cannot be reduced, but also the appearance of the molded product deteriorates. Furthermore, heat treatment time
It can be seen that the compression set cannot be reduced if it is too short, 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, the compression set can be significantly reduced.

【0053】[0053]

【発明の効果】本発明の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。
EFFECTS OF THE INVENTION The soft vinyl chloride foamed molded product of the present invention is characterized in that it has a uniform expansion of cells and excellent independence while having a foaming ratio of 1.2 times or more, and has a small permanent set. .

【0054】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 foamed molded product which is excellent in sound insulation properties, vibration isolation properties, heat insulation properties, protection properties, sealing properties and cushioning properties. Furthermore, the extrusion molding method makes it possible to inexpensively and easily produce a molded product having an excellent appearance, and can be sufficiently used even in the fields where only foams of EPDM and polyurethane rubber have been conventionally used. it can.

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

【図1】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である。
FIG. 1 is an explanatory view showing a 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.

【図2】図1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. 2 is an explanatory diagram showing a method of measuring compression set using a test piece manufactured using the mold shown in FIG.

Claims (1)

【特許請求の範囲】[Claims] 1 塩化ビニル系樹脂100重量部に対して、メチルエ
チルケトンに5〜90重量%溶解するアクリロニトリル
―ブタジエンゴム5〜150重量部、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1〜60重量部および可
塑剤20〜200重量部を含む軟質塩化ビニル系樹脂組
成物から成形された発泡倍率1.2〜2.5倍で永久歪
15〜40%の軟質塩化ビニル系発泡成形品。
1. 100 ml of benzene containing 100 parts by weight of vinyl chloride resin, 5 to 150 parts by weight of acrylonitrile-butadiene rubber dissolved in methyl ethyl ketone in an amount of 5 to 90% by weight, and 100 ml of benzene containing 0.4 g of a copolymer containing methyl methacrylate as a main component. Expansion ratio molded from a soft vinyl chloride resin composition containing 1 to 60 parts by weight of a methyl methacrylate copolymer having a specific viscosity of 2.5 or more measured at 30 ° C. and a plasticizer of 20 to 200 parts by weight. Flexible vinyl chloride foamed molded product with 1.2 to 2.5 times and permanent strain of 15 to 40 % .
JP5233233A 1986-09-11 1993-09-20 Flexible vinyl chloride foamed molded product with small permanent set Expired - Fee Related JPH07107106B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5233233A JPH07107106B2 (en) 1986-09-11 1993-09-20 Flexible vinyl chloride foamed molded product with small permanent set

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP61214690A JPH0657759B2 (en) 1986-09-11 1986-09-11 Manufacturing method of soft vinyl chloride foam moldings with small permanent set
JP5233233A JPH07107106B2 (en) 1986-09-11 1993-09-20 Flexible vinyl chloride foamed molded product with small permanent set

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP61214690A Division JPH0657759B2 (en) 1986-09-11 1986-09-11 Manufacturing method of soft vinyl chloride foam moldings with small permanent set

Publications (2)

Publication Number Publication Date
JPH06192457A JPH06192457A (en) 1994-07-12
JPH07107106B2 true JPH07107106B2 (en) 1995-11-15

Family

ID=26520457

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5233233A Expired - Fee Related JPH07107106B2 (en) 1986-09-11 1993-09-20 Flexible vinyl chloride foamed molded product with small permanent set

Country Status (1)

Country Link
JP (1) JPH07107106B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3568477B2 (en) * 1998-02-24 2004-09-22 三菱レイヨン株式会社 Processing aid for foam molding and vinyl chloride resin composition using the same

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6011974B2 (en) * 1979-05-21 1985-03-29 三菱化成ポリテック株式会社 Expandable vinyl chloride resin composition
JPS6166732A (en) * 1984-09-10 1986-04-05 Kanegafuchi Chem Ind Co Ltd Resin composition for extrusion molding of profile
JPS61195144A (en) * 1985-02-26 1986-08-29 Mitsubishi Monsanto Chem Co Production of thermoplastic elastomer of vinyl chloride resin
JPS62187742A (en) * 1986-02-13 1987-08-17 Shin Etsu Polymer Co Ltd Expandable vinyl chloride resin composition

Also Published As

Publication number Publication date
JPH06192457A (en) 1994-07-12

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