JPH02196618A - Production of resin foamed sheet - Google Patents
Production of resin foamed sheetInfo
- Publication number
- JPH02196618A JPH02196618A JP1017320A JP1732089A JPH02196618A JP H02196618 A JPH02196618 A JP H02196618A JP 1017320 A JP1017320 A JP 1017320A JP 1732089 A JP1732089 A JP 1732089A JP H02196618 A JPH02196618 A JP H02196618A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- hollow
- extrusion
- molten resin
- hollow body
- 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.)
- Pending
Links
Landscapes
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
本発明は気泡が均一に分散した樹脂発泡シートを!!逍
する方法に関する。The present invention provides a resin foam sheet with evenly dispersed air bubbles! ! Concerning how to attend.
従来上り、発泡性溶融樹脂を押出し成形して樹脂発泡シ
ートが製造されている。Conventionally, foamed resin sheets have been manufactured by extrusion molding a foamable molten resin.
発泡性溶融樹脂1を押出し成形する場合には、第4図に
示すように押出ダイ4を出たシート状の樹脂発泡体2は
膨張してしまっていた。これは、矢印で示すように気泡
に外方への応力が働くからであり、このため、異常発泡
が発生してしまい、気泡が均一に分散しないだけでなく
、外皮が形成されないという問題があった。
本発明は上記課題を解決するために為されたものであり
、その目的とするところは、気泡が均一に分散し、外皮
も形成されている甜脂発泡シートを製造することにある
。When the foamable molten resin 1 is extruded, the sheet-shaped resin foam 2 exiting the extrusion die 4 has expanded as shown in FIG. This is because outward stress is applied to the bubbles as shown by the arrows, which causes abnormal foaming, which not only prevents the bubbles from dispersing uniformly but also prevents the formation of a skin. Ta. The present invention has been made to solve the above problems, and its purpose is to produce a sugar beet foam sheet in which air bubbles are uniformly dispersed and a skin is also formed.
【課題を解決するための手段1
本発明の樹脂発泡シートの製造方法は、発泡性溶融樹I
yIt1を中空体状に押出し成形し、次いでこの中空の
樹脂発泡体2を圧着させて中実のシート状に成形するこ
とを特徴とするものであり、この構成により上記課題が
解決されたものである。
【作用1
発泡性溶融樹脂1を中空体状に押出し成形するので、発
泡により生じる応力が外方と中空方向に加わり、気泡を
均一に分散させることができるものであり、この中空体
の樹脂発泡体2を圧着させて中実のシート状に形成する
ので、気泡が均一に分散し、しかも外皮3が形成された
樹脂発泡シートAを製造することができるものである。
[*施例1
本発明において使用する発泡性溶融樹脂1としては、熱
可塑性樹脂に発泡剤を配合させたものであればとくに制
限がない0例えば、熱可塑性樹脂としては塩化ビニル樹
脂、ポリスチレン樹脂、ABS樹脂、低密度、中密度、
高密度のポリエチレン樹脂、ポリプロピレン樹脂、エチ
レンとプロピレン、酢酸ビニル、メチルメタクリレート
、アクリル酸等の共重合樹脂等を単独又は混合して使用
される0発泡剤としては、ジクロロテトラフルオロエタ
ン、シクaロシフルオロメタン、トリクロロフルオロメ
タン、プロパン、ブタン、又はこれらと塩化メチル、塩
化メチレン、ペンタン、ヘキサン等との混合物、更には
アゾシカ−ボンアマイド(ADCA)などの化学分解型
のものが使用される。その他、必要に応じて気泡調節剤
、各種滑剤等の添加剤等が配合される。
この発泡性溶融樹脂1が押出機Bにより押し出される。
押出ダイ4の内部には中子5が配置されており、発泡性
溶融樹脂1は発泡して中空体状に押し出し成形される。
この場合、第3図に示すように、発泡剤が発泡して生じ
る応力は矢印で示すように外方と中子5方向である中空
方向に加わり、気泡が均一に分散されると共に外皮3が
形成される6次いで、この中空の樹脂発泡体2はランド
6を経てコントロールへラド7に送られる。コントロー
ルヘッド7は押出ダイ4におけるよりも数十度低い温度
に設定されている。このフントロールへラド7により中
空の樹脂発泡体2は圧着されて、中実のシート状に成形
され樹脂発泡シー)Aが製造される。コントロールへラ
ド7の温度をiqvすることにより発泡倍率、即ち、密
度が調整されるものである。
例えば、塩化ビニル樹脂92.7重量%、充填材5.0
重量%、顔料(チタン)2重量%、発泡剤(ADCA)
0.3重量%が配合され、押出ダイ4の温度が180℃
で押出速度が600〜900 aml論in、発泡倍率
(密度)0.5〜0.9で押出し成形される。この場合
、コントロールへラド7の温度ハ約−20℃の150〜
160”Cに設定される。これにより、外皮3が形成さ
れた塩化ビニル樹脂発泡シートAが得られる。
【発明の効果】
本発明にあっては発泡性溶融樹脂を中空体状に押出し成
形し、次いでこの中空体の樹脂発泡体を圧着させて中実
のシート状に成形するので、発泡により生じる応力が外
方と中空方向に加わり、気泡を均一に分散させることが
できるものであり、更に、この中空体の樹脂発泡体を圧
着させて中実のシート状に形成するので、気泡が均一に
分散し、しかも外皮が形成された樹脂発泡シートを製造
することができるものである。[Means for Solving the Problems 1] The method for producing a resin foam sheet of the present invention includes foamable melt resin I
The feature is that yIt1 is extruded into a hollow body shape, and then this hollow resin foam 2 is pressed and molded into a solid sheet shape, and this structure solves the above problems. be. [Effect 1] Since the foamable molten resin 1 is extruded into a hollow body shape, the stress generated by foaming is applied outward and in the hollow direction, and the air bubbles can be uniformly dispersed. Since the body 2 is pressed and formed into a solid sheet, a resin foam sheet A can be manufactured in which air bubbles are uniformly dispersed and an outer skin 3 is formed. [*Example 1 The foamable molten resin 1 used in the present invention is not particularly limited as long as it is a thermoplastic resin mixed with a blowing agent. For example, the thermoplastic resin may include vinyl chloride resin, polystyrene resin, etc. , ABS resin, low density, medium density,
Examples of blowing agents used alone or in combination include high-density polyethylene resin, polypropylene resin, copolymer resins of ethylene and propylene, vinyl acetate, methyl methacrylate, acrylic acid, etc. Fluoromethane, trichlorofluoromethane, propane, butane, or mixtures of these with methyl chloride, methylene chloride, pentane, hexane, etc., and chemically decomposed ones such as azocica-bonamide (ADCA) are used. In addition, additives such as a bubble control agent and various lubricants may be added as necessary. This foamable molten resin 1 is extruded by an extruder B. A core 5 is disposed inside the extrusion die 4, and the foamable molten resin 1 is foamed and extruded into a hollow body shape. In this case, as shown in FIG. 3, the stress generated by the foaming of the foaming agent is applied to the outside and the hollow direction, which is the direction of the core 5, as shown by the arrows, so that the bubbles are uniformly dispersed and the outer skin 3 is The formed hollow resin foam 2 is then sent to the control pad 7 via the land 6. The temperature of the control head 7 is set to several tens of degrees lower than that of the extrusion die 4. The hollow resin foam 2 is crimped by the mount roll 7 and molded into a solid sheet, thereby producing a resin foam sheet (A). The foaming ratio, that is, the density is adjusted by changing the temperature of the control pad 7 to iqv. For example, vinyl chloride resin 92.7% by weight, filler 5.0%
Weight%, pigment (titanium) 2% by weight, blowing agent (ADCA)
0.3% by weight is blended, and the temperature of extrusion die 4 is 180°C.
Extrusion molding is carried out at an extrusion speed of 600 to 900 AML and an expansion ratio (density) of 0.5 to 0.9. In this case, the temperature of the control controller 7 is 150 to about -20°C.
160"C. As a result, a vinyl chloride resin foam sheet A with an outer skin 3 formed thereon is obtained. [Effects of the Invention] In the present invention, a foamable molten resin is extruded into a hollow body shape. Then, this hollow resin foam is pressed and molded into a solid sheet, so the stress generated by foaming is applied outward and in the hollow direction, making it possible to uniformly disperse the air bubbles. Since this hollow resin foam is pressed and formed into a solid sheet, it is possible to manufacture a resin foam sheet in which air bubbles are uniformly dispersed and an outer skin is formed.
$1図は本発明の一実施例の工程を示す概略断面図、第
2図はtIII1図のX−X断面図、第3図は同上の作
用を示す説明図、第4図は従来例を示す概略断面図であ
って、Aは樹脂発泡シート、Bは押出機、1は発泡性溶
融樹脂、2は樹脂発泡体、3は外皮、4は押出ダイ、5
は中子、6はランド、7はコントロールヘッドである。
代理人 弁理士 石 1)艮 七
第2WJ
第3図
第4
図Figure 1 is a schematic sectional view showing the process of an embodiment of the present invention, Figure 2 is a sectional view taken along line X-X of Figure tIII1, Figure 3 is an explanatory view showing the same effect, and Figure 4 is a diagram showing the conventional example. 1 is a schematic cross-sectional view showing a foamed resin sheet, B is an extruder, 1 is a foamable molten resin, 2 is a resin foam, 3 is an outer skin, 4 is an extrusion die, and 5 is a schematic cross-sectional view.
is a core, 6 is a land, and 7 is a control head. Agent Patent Attorney Ishi 1) Ai 7th 2nd WJ Figure 3 Figure 4
Claims (2)
でこの中空体の樹脂発泡体を圧着させて中実のシート状
に成形することを特徴とする樹脂発泡シートの製造方法
。(1) A method for producing a resin foam sheet, which comprises extruding and L-molding a foamable molten resin into a hollow body, and then press-bonding the hollow resin foam to form a solid sheet.
で圧着させることを特徴とする請求項1記載の樹脂発泡
シートの製造方法。(2) The method for producing a resin foam sheet according to claim 1, characterized in that the hollow resin foam is compressed at a temperature lower than the extrusion molding temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1017320A JPH02196618A (en) | 1989-01-26 | 1989-01-26 | Production of resin foamed sheet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1017320A JPH02196618A (en) | 1989-01-26 | 1989-01-26 | Production of resin foamed sheet |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02196618A true JPH02196618A (en) | 1990-08-03 |
Family
ID=11940736
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1017320A Pending JPH02196618A (en) | 1989-01-26 | 1989-01-26 | Production of resin foamed sheet |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02196618A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2019188669A (en) * | 2018-04-23 | 2019-10-31 | 株式会社イノアックコーポレーション | Method for producing foam laminate sheet |
-
1989
- 1989-01-26 JP JP1017320A patent/JPH02196618A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2019188669A (en) * | 2018-04-23 | 2019-10-31 | 株式会社イノアックコーポレーション | Method for producing foam laminate sheet |
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