JPH0571019B2 - - Google Patents

Info

Publication number
JPH0571019B2
JPH0571019B2 JP62202568A JP20256887A JPH0571019B2 JP H0571019 B2 JPH0571019 B2 JP H0571019B2 JP 62202568 A JP62202568 A JP 62202568A JP 20256887 A JP20256887 A JP 20256887A JP H0571019 B2 JPH0571019 B2 JP H0571019B2
Authority
JP
Japan
Prior art keywords
resin
parts
vinyl chloride
laminate
chloride resin
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 - Lifetime
Application number
JP62202568A
Other languages
Japanese (ja)
Other versions
JPS6444724A (en
Inventor
Yoshinori Ueda
Kazuhiko Kise
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.)
Fukubi Kagaku Kogyo KK
Original Assignee
Fukubi Kagaku Kogyo KK
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 Fukubi Kagaku Kogyo KK filed Critical Fukubi Kagaku Kogyo KK
Priority to JP62202568A priority Critical patent/JPS6444724A/en
Publication of JPS6444724A publication Critical patent/JPS6444724A/en
Publication of JPH0571019B2 publication Critical patent/JPH0571019B2/ja
Granted legal-status Critical Current

Links

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  • Laminated Bodies (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、強固にかつ均一に一体化された、塩
化ビニル樹脂と発泡性スチレン系樹脂との共押出
し成形積層体を、能率よく低廉に製造可能とす
る、共押出し成形積層体の製造方法に関するもの
である。
Detailed Description of the Invention (Field of Industrial Application) The present invention efficiently and inexpensively produces a coextrusion molded laminate of vinyl chloride resin and expandable styrene resin that is firmly and uniformly integrated. The present invention relates to a method for manufacturing a coextrusion laminate that can be manufactured.

(従来技術及び発明が解決しようとする問題点) 例えば天井材として用いられる合成樹脂製の積
層断熱板を例にとると、該積層断熱板は、従来、
樹脂基板を一旦形成した後、該樹脂基板に発泡樹
脂板を、接着剤あるいは両面粘着テープを用いて
接着固定することにより製作されていた。そし
て、積層板の素材としては、該積層板を、経済
性、剛性、断熱性等に優れたものとするため、樹
脂基板の素材として塩化ビニル樹脂を採用すると
ともに発泡樹脂板の素材として発泡性スチレン系
樹脂を採用するのが一般的であつた。
(Prior Art and Problems to be Solved by the Invention) For example, if we take a synthetic resin laminated heat insulating board used as a ceiling material, the laminated heat insulating board has conventionally
After a resin substrate is once formed, a foamed resin plate is adhesively fixed to the resin substrate using an adhesive or double-sided adhesive tape. As the material for the laminate, in order to make the laminate excellent in economy, rigidity, heat insulation, etc., vinyl chloride resin is used as the material for the resin substrate, and foaming resin is used as the material for the foamed resin board. It was common to use styrene resin.

ところで、樹脂基板と発泡樹脂板とを接着剤を
用いて固定する手段により一体化して積層板を製
作する従来の方法にあつては、接着剤の均一な塗
布が困難であつて接着不良部分が発生しやすく、
長年のうちには樹脂基板と発泡樹脂板とが部分的
に剥離して所期の断熱効果等が発揮されなくなる
という問題があつた。又接着一体化の手段にあつ
ては、接着剤の塗布作業に困難を伴うことから、
製作しうる積層板の幅には限界があり、あまり広
幅の積層板は製作が非常に困難であつた。さらに
は、接着剤の塗布作業に手間を要して生産性が悪
かつた他、接着剤が高価につくことも加わつて、
積層板の製造コストの上昇を招くという問題もあ
つた。又、樹脂基板と発泡樹脂板とを両面粘着テ
ープを用いて固定する手段により一体化して積層
板を製作する従来方法にあつては、生産効率が悪
いとともに両面粘着テープが高価であることから
製造コストの上昇を招く問題があつた。
By the way, in the conventional method of manufacturing a laminate by integrating a resin substrate and a foamed resin board by fixing them using an adhesive, it is difficult to apply the adhesive uniformly, and there are areas with poor adhesion. It is easy to occur,
Over the years, there has been a problem in that the resin substrate and the foamed resin board partially peel off and the desired heat insulation effect is no longer achieved. In addition, when it comes to adhesive integration, it is difficult to apply the adhesive, so
There is a limit to the width of laminates that can be manufactured, and it has been extremely difficult to manufacture laminates that are too wide. Furthermore, the process of applying the adhesive was labor-intensive, resulting in poor productivity, and the adhesive was also expensive.
Another problem was that the manufacturing cost of the laminate increased. In addition, the conventional method of manufacturing a laminate by integrating a resin substrate and a foamed resin board by fixing them using double-sided adhesive tape has poor production efficiency and is difficult to manufacture due to the high cost of double-sided adhesive tape. There was a problem that led to an increase in costs.

このような別部材の接着一体化には、以上述べ
たような問題があつたことから、これに代え、塩
化ビニル樹脂と発泡性スチレン系樹脂とを共押出
しすることによつて、目的とする積層板を製造せ
んとする試みも一部で行われている。なお、該共
押出し成形においては、塩化ビニル樹脂と発泡性
スチレン系樹脂との密着性が悪いために、共押出
しの際、樹脂間界面に接着剤を介在させることが
必須となる。しかしながら、接着剤を介在させて
のかかる共押出しの手段によるばあいには、積層
板を連続的に製造できて生産性向上を期しうる長
所がある反面、次のような回避し難い問題があ
り、実用化はかなり困難とされている。
Since the above-mentioned problems existed in bonding and integrating separate parts, we decided to co-extrude vinyl chloride resin and expandable styrene resin to achieve the desired goal. Some attempts have also been made to manufacture laminates. In addition, in the coextrusion molding, since the adhesiveness between the vinyl chloride resin and the expandable styrene resin is poor, it is essential to interpose an adhesive at the interface between the resins during coextrusion. However, such coextrusion using an adhesive has the advantage of being able to continuously manufacture laminates and improving productivity, but it also has the following unavoidable problems: , it is considered to be quite difficult to put it into practical use.

まず第1には、均一な品質(特に、接着力のバ
ラツキがないこと)を有する積層板を安定的に生
産することが困難である問題があつた。
First of all, there was a problem in that it was difficult to stably produce a laminate having uniform quality (particularly, no variation in adhesive strength).

即ち、塩化ビニル樹脂、発泡性スチレン系樹脂
及び接着剤の三種の樹脂を金型内において合流さ
せる必要があることから、金型の構造が複雑なも
のとなり、その結果、樹脂の滞留が生じて樹脂焼
付き等が発生しやすいこと;又、樹脂押出し用の
押出成形機二台に加え、接着剤用の押出成形機が
更に一台必要となることから、二台の押出成形機
を対象とするばあいに比べ、流量バランスの制御
の困難性が倍加すること;さらには、塩化ビニル
樹脂、発泡性スチレン系樹脂及び接着剤の夫々の
適性温度条件が異なるとともに、接着剤の各種の
挙動因子が二種の樹脂の接着性に複雑な影響を及
ぼす等、押出成形上の制約条件が多いこと;など
から、均一な品質を有する積層板を安定的に生産
することが困難であつたのである。
In other words, it is necessary to combine three types of resins, vinyl chloride resin, expandable styrene resin, and adhesive, in the mold, which makes the structure of the mold complicated, and as a result, resin stagnation occurs. Resin seizure is likely to occur; in addition, in addition to two extrusion molding machines for resin extrusion, an additional extrusion molding machine for adhesive is required, so two extrusion molding machines are targeted. In addition, the difficulty in controlling the flow rate balance is doubled compared to the case where the flow balance is It has been difficult to stably produce laminates with uniform quality due to the many constraints on extrusion molding, such as the fact that .

第2には、製造コストが非常に高く付く問題が
あつた。
Second, there was the problem that manufacturing costs were extremely high.

即ち、三台の押出成形機を必要とするため、製
造物の付加価値の割には設備費が高くつくこと;
三台の押出成形機を設置するための相当広いスペ
ースを要すること;又三台の押出成形機を正しく
制御(流量バランスの制御や適性温度条件の制御
等)するための制御装置が必要になること;さら
には金型が複雑であることからその製作費が高く
つき、又接着剤が高価であること;などから、製
造コストが非常に高くつく問題があつたのであ
る。
That is, since three extrusion molding machines are required, the equipment cost is high compared to the added value of the product;
A fairly large space is required to install the three extrusion molding machines; a control device is also required to properly control the three extrusion molding machines (controlling the flow rate balance, controlling the appropriate temperature conditions, etc.) Moreover, the manufacturing cost was high because the mold was complicated, and the adhesive was expensive, which caused the problem of extremely high manufacturing costs.

本発明者は、前記した問題点をつぶさに検討し
た結果、これらの問題点は、「樹脂間界面に接着
剤を介在させて両樹脂の一体化を図ろうとする」
ことに帰因するものであり、いずれか一方の樹脂
を、それが他方の樹脂との相溶性に富むものに改
質したならば、両樹脂の共押出しにともなう前記
諸問題点が一挙に解決されるのではないかとの知
見を得た。
As a result of a detailed study of the above-mentioned problems, the inventor of the present invention found that these problems can be solved by ``attempting to integrate both resins by interposing an adhesive at the interface between the two resins.''
This is due to the fact that if one of the resins is modified to be highly compatible with the other resin, the aforementioned problems associated with coextrusion of both resins can be solved at once. We have obtained knowledge that this may be the case.

本発明は、かかる知見をさらに発展させること
によつて完成されたものである。
The present invention was completed by further developing this knowledge.

(問題点を解決するための手段) 本発明に係る共押出し成形積層体の製造方法
(以下製造方法という)は、塩化ビニル樹脂と;
アクリル系樹脂及び/又は酢酸ビニル系樹脂を用
いた改質剤の配合により該塩化ビニル樹脂との相
溶性が向上せしめられた改質発泡性スチレン系樹
脂と;を共押出して、両樹脂の積層体(板状積層
体、チヤンネル状積層体等、各種の形態を有する
積層体)を製造することを特徴とするものであ
る。
(Means for Solving the Problems) A method for manufacturing a coextrusion laminate according to the present invention (hereinafter referred to as a manufacturing method) comprises: a vinyl chloride resin;
A modified foamable styrenic resin whose compatibility with the vinyl chloride resin has been improved by blending a modifier with an acrylic resin and/or a vinyl acetate resin; and a lamination of both resins. This method is characterized by manufacturing bodies (laminates having various forms such as plate-like laminates and channel-like laminates).

(実施例) 以下本発明の実施例を説明する。(Example) Examples of the present invention will be described below.

本発明の製造方法は、塩化ビニル樹脂と改質発
泡性スチレン系樹脂とを共押出しして所要の積層
体を製造するものである。
The manufacturing method of the present invention is to co-extrude a vinyl chloride resin and a modified expandable styrene resin to manufacture a desired laminate.

改質剤としては、前記相溶性向上効果に優れる
とともに、比較的安価に入手しうる、アクリル系
樹脂あるいは酢酸ビニル系樹脂を挙げることがで
きる。該アクリル系樹脂改質剤としては、メチル
メタクリレート樹脂、メチルメタクリレート・ブ
タジエン・スチレン三元共重合体、アクリロニト
リル・スチレン共重合体、アクリロニトリル・ブ
タジエン・スチレン三元共重合体、塩素化ポリエ
チレンあるいはNBR、SBR等の合成ゴムを好適
に採用でき、又酢酸ビニル系樹脂改質剤として
は、エチレン酢酸ビニル共重合体を好適に採用で
きる。
Examples of the modifier include acrylic resins and vinyl acetate resins, which have the above-mentioned compatibility-improving effect and are available at relatively low cost. The acrylic resin modifier includes methyl methacrylate resin, methyl methacrylate-butadiene-styrene terpolymer, acrylonitrile-styrene copolymer, acrylonitrile-butadiene-styrene terpolymer, chlorinated polyethylene or NBR, Synthetic rubber such as SBR can be suitably employed, and ethylene-vinyl acetate copolymer can be suitably employed as the vinyl acetate resin modifier.

次に、塩化ビニル樹脂押出素材(塩化ビニル樹
脂を主成分とする)と発泡性スチレン系樹脂押出
素材(スチレン系樹脂を主成分とする)の配合例
を示す。なお、以下の配合例において、「部」と
は重量部をいう。
Next, a blending example of a vinyl chloride resin extruded material (mainly composed of vinyl chloride resin) and a foamable styrene resin extruded material (mainly composed of styrene resin) will be shown. In addition, in the following formulation examples, "parts" refer to parts by weight.

塩化ビニル樹脂押出素材の配合例(1) 塩化ビニル樹脂: 100部 安定剤: 3〜5部 滑 剤: 0.5〜3部 充填剤: 5〜20部 着色剤: 0.5〜2.0部 塩化ビニル樹脂押出素材の配合例(2) 塩化ビニル樹脂: 100部 有機系発泡剤: 0.3〜0.5部 安定剤: 3〜5部 滑 剤: 0.5〜3部 充填剤: 5〜20部 着色剤: 0.5〜2.0部 発泡性スチレン系樹脂押出素材の配合例(1) 発泡性ポリスチレン: 90部 アクリロニトリル・スチレン共重合体(改質
剤): 10部 タルク: 0.5部 無機系発泡剤: 0.5部 発泡性スチレン系樹脂押出素材の配合例(2) 発泡性ポリスチレン: 100部 ポリメチルメタアクリレート(改質剤):
3〜5部 タルク: 0.5部 無機系発泡剤: 0.5部 発泡性スチレン系樹脂押出素材の配合例(3) 発泡性ポリスチレン: 100部 エチレン酢酸ビニル共重合体(改質剤):
3〜5部 タルク: 0.5部 無機系発泡剤: 0.5部 発泡性スチレン系樹脂押出素材の配合例(4) 発泡性ポリスチレン: 90部 アクリロニトリル・スチレン共重合体(改質
剤): 10部 エチレン酢酸ビニル共重合体(改質剤): 5部 ポリメチルメタアクリレート(改質剤): 1部 タルク: 0.5部 無機系発泡剤: 0.5部 以上のように配合された二種類の押出素材を、
二台の押出成形機の夫々に供給して共押出し成形
すると、発泡性スチレン系樹脂が塩化ビニル樹脂
との相溶性に富むものに改質されていることか
ら、例えば第1図に示すごとき、塩化ビニル樹脂
製の樹脂基板2と発泡性スチレン系樹脂製の発泡
樹脂板3(発泡倍率は例えば5〜15倍程度)とが
強固かつ均一に一体化した、断熱性及び剛性に優
れる積層体1が連続的に製造されることとなる。
Blend example of vinyl chloride resin extrusion material (1) Vinyl chloride resin: 100 parts Stabilizer: 3 to 5 parts Lubricant: 0.5 to 3 parts Filler: 5 to 20 parts Colorant: 0.5 to 2.0 parts Vinyl chloride resin extrusion material Blend example (2) Vinyl chloride resin: 100 parts Organic blowing agent: 0.3 to 0.5 parts Stabilizer: 3 to 5 parts Lubricant: 0.5 to 3 parts Filler: 5 to 20 parts Colorant: 0.5 to 2.0 parts Foaming Compounding example of extruded styrenic resin material (1) Expandable polystyrene: 90 parts Acrylonitrile-styrene copolymer (modifier): 10 parts Talc: 0.5 part Inorganic blowing agent: 0.5 part Expandable styrenic resin extruded material Blend example (2) Expandable polystyrene: 100 parts polymethyl methacrylate (modifier):
3 to 5 parts Talc: 0.5 parts Inorganic blowing agent: 0.5 parts Formulation example of expandable styrenic resin extrusion material (3) Expandable polystyrene: 100 parts Ethylene-vinyl acetate copolymer (modifier):
3 to 5 parts Talc: 0.5 parts Inorganic blowing agent: 0.5 parts Compounding example of expandable styrenic resin extrusion material (4) Expandable polystyrene: 90 parts Acrylonitrile-styrene copolymer (modifier): 10 parts Ethylene acetic acid Vinyl copolymer (modifier): 5 parts Polymethyl methacrylate (modifier): 1 part Talc: 0.5 part Inorganic blowing agent: 0.5 part The two types of extrusion materials blended as above,
When fed to each of two extrusion molding machines and coextruded, the foamable styrene resin has been modified to be highly compatible with the vinyl chloride resin, so for example, as shown in Figure 1, A laminate 1 with excellent heat insulation and rigidity, in which a resin substrate 2 made of vinyl chloride resin and a foamed resin board 3 made of foamed styrene resin (expansion ratio is, for example, about 5 to 15 times) are firmly and uniformly integrated. will be manufactured continuously.

なお、塩化ビニル樹脂押出素材については、有
機系発泡剤含有の有無を問わないが、前記塩化ビ
ニル樹脂押出素材の配合例(2)に示すごとく、有機
系発泡剤を0.3〜0.5部程度含有させて塩化ビニル
樹脂を2倍程度の発泡体とするばあいには、樹脂
基板成形時の発泡圧によつて、樹脂基板と発泡樹
脂板とが当接面において強く圧着されることとな
り、しかも、該発泡によつて樹脂基板の当接面が
荒れた状態となることから、これによるアンカー
作用も発揮されることとなり、樹脂基板と発泡樹
脂板とが、一層強固にかつ均一に一体化した積層
体が得られることとなる。
Note that the extruded vinyl chloride resin material may or may not contain an organic blowing agent, but as shown in the formulation example (2) of the extruded vinyl chloride resin material, it may contain about 0.3 to 0.5 parts of an organic blowing agent. In the case where the vinyl chloride resin is made into a foam of about twice the size, the foaming pressure during molding of the resin substrate causes the resin substrate and the foamed resin plate to be strongly pressed together at the contact surfaces, and furthermore, Since the contact surface of the resin substrate becomes rough due to the foaming, this also exerts an anchoring effect, resulting in a laminated structure in which the resin substrate and the foamed resin board are integrated more firmly and uniformly. The body will be obtained.

(発明の効果) 本発明に係る製造方法は、塩化ビニル樹脂と、
該樹脂との相溶性に優れる改質発泡性スチレン系
樹脂とを共押出しするため、塩化ビニル樹脂と発
泡性スチレン系樹脂とが強固にかつ均一に一体化
された共押出し成形積層体を能率よく低廉に製造
することができる。
(Effect of the invention) The manufacturing method according to the present invention includes a vinyl chloride resin,
In order to coextrude a modified expandable styrene resin that has excellent compatibility with the resin, we can efficiently produce a coextrusion molded laminate in which vinyl chloride resin and expandable styrenic resin are firmly and uniformly integrated. It can be manufactured at low cost.

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

第1図は本発明の製造方法によつて製造された
積層体を例示する斜視図である。 1……積層体、2……樹脂基板、3……発泡樹
脂板。
FIG. 1 is a perspective view illustrating a laminate manufactured by the manufacturing method of the present invention. 1... Laminated body, 2... Resin substrate, 3... Foamed resin board.

Claims (1)

【特許請求の範囲】[Claims] 1 塩化ビニル樹脂と;アクリル系樹脂及び/又
は酢酸ビニル系樹脂を用いた改質剤の配合により
該塩化ビニル樹脂との相溶性が向上せしめられた
改質発泡性スチレン系樹脂と;を共押出して、両
樹脂の積層体を製造することを特徴とする、共押
出し成形積層体の製造方法。
1. Coextrusion of a vinyl chloride resin and a modified expandable styrenic resin whose compatibility with the vinyl chloride resin has been improved by blending a modifier with an acrylic resin and/or a vinyl acetate resin. A method for producing a coextrusion-molded laminate, comprising: producing a laminate of both resins.
JP62202568A 1987-08-12 1987-08-12 Preparation of coextrusion molded laminate Granted JPS6444724A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62202568A JPS6444724A (en) 1987-08-12 1987-08-12 Preparation of coextrusion molded laminate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62202568A JPS6444724A (en) 1987-08-12 1987-08-12 Preparation of coextrusion molded laminate

Publications (2)

Publication Number Publication Date
JPS6444724A JPS6444724A (en) 1989-02-17
JPH0571019B2 true JPH0571019B2 (en) 1993-10-06

Family

ID=16459653

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62202568A Granted JPS6444724A (en) 1987-08-12 1987-08-12 Preparation of coextrusion molded laminate

Country Status (1)

Country Link
JP (1) JPS6444724A (en)

Also Published As

Publication number Publication date
JPS6444724A (en) 1989-02-17

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