JPH1034753A - Manufacture of molding having high density skin layer - Google Patents

Manufacture of molding having high density skin layer

Info

Publication number
JPH1034753A
JPH1034753A JP9113338A JP11333897A JPH1034753A JP H1034753 A JPH1034753 A JP H1034753A JP 9113338 A JP9113338 A JP 9113338A JP 11333897 A JP11333897 A JP 11333897A JP H1034753 A JPH1034753 A JP H1034753A
Authority
JP
Japan
Prior art keywords
steam
resin particles
particles
mold
skin layer
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
Application number
JP9113338A
Other languages
Japanese (ja)
Inventor
Koji Shinto
幸治 新堂
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.)
Mitsubishi Chemical BASF Co Ltd
Original Assignee
Mitsubishi Chemical BASF Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Chemical BASF Co Ltd filed Critical Mitsubishi Chemical BASF Co Ltd
Priority to JP9113338A priority Critical patent/JPH1034753A/en
Publication of JPH1034753A publication Critical patent/JPH1034753A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To reduce contraction even for a body of complex shape and to improve its appearance by a method in which when the surface pressure of foamed resin particles packed in a cavity has reached a specified pressure range, air among the particles is discharged, and the steam of a temperature below the melting point of the resin is introduced among the particles from a steam chamber. SOLUTION: When the surface pressure of foamed resin particles packed in a cavity 3 has reached 0.01-1.5kg/cm<2> G, a vacuum conduit 7 valve is opened, a drain conduit 9 valve is closed, a steam chamber 1a and the cavity 3 are evacuated to discharge air among the particles. After that, the vacuum conduit 7 valve is closed, and steam of a temperature necessary for the fusion bonding of the particles in a mold is introduced from a steam conduit 6 to heat the particles. The steam passes through the chamber 1a from the conduit 6, flows into the cavity 3 through a steam hole 1a, and heats the particles. In this process, the steam also behaves as a heating medium for heating a molding mold.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、高密度のスキン層
を持つ成形体の製造方法に関し、詳しくは、成形体の表
面部に均一かつ高密度で硬いスキン層を備えた収縮の少
ない成形体の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a molded article having a high-density skin layer, and more particularly, to a molded article having a uniform, high-density, hard skin layer on the surface of the molded article and having a small shrinkage. And a method for producing the same.

【0002】[0002]

【従来の技術】各々水蒸気室を備えたキャビ型およびコ
ア型から成る発泡成形用金型のキャビティ内に発泡樹脂
粒子(以下、発泡粒子という)を充填し加熱融着させて
製造される成形体は、独立気泡構造を備え且つ断熱性お
よび緩衝性に富み、しかも、軽いという特徴を有し、緩
衝材、断熱材、断熱容器、機能部材などに使用されてい
る。
2. Description of the Related Art Molded articles produced by filling foamed resin particles (hereinafter referred to as "foamed particles") in a cavity of a foaming mold composed of a mold cavity and a core mold each having a steam chamber and heat-sealing them. Is characterized by having a closed-cell structure, being rich in heat insulation and buffering properties, and light in weight, and is used for cushioning materials, heat insulating materials, heat insulating containers, functional members, and the like.

【0003】しかしながら、成形体の表面には粒子間の
間隙が僅かに残っているため、容器などの用途において
繰り返し使用した場合、粒子間の間隙に汚れが入ると共
に割れ易く、また、成形体表面部が柔らかいために傷が
付き易いと言う問題がある。そのため、従来の製造方法
においては、容器内面をコーティングする方法や樹脂シ
ート等と一体成形する方法を採用せざるを得ず、得られ
る成形体のコストが高いと言う問題がある。
[0003] However, since a small gap between the particles remains on the surface of the molded article, when used repeatedly in applications such as a container, the gap between the particles becomes dirty and easily cracks. There is a problem that the part is soft and easily scratched. Therefore, in the conventional manufacturing method, a method of coating the inner surface of the container or a method of integrally molding with a resin sheet or the like has to be adopted, and there is a problem that the cost of the obtained molded body is high.

【0004】これらの問題を解決するため、例えば、特
開昭48−28060号公報、特開昭52−47866
号公報などには、成形加工時、成形体の表面部に溶融に
よりスキン層を形成する方法が提案されている。これら
の成形方法においては、各々水蒸気室を備えたキャビ型
およびコア型から成り、各水蒸気室のキャビティに面す
る壁面には多数の蒸気孔が形成された発泡成形用金型を
使用し、キャビティ内に発泡粒子を充填し、発泡粒子の
溶融温度未満の水蒸気を水蒸気室に導入して発泡粒子同
士を加熱融着させて成形体とした後、さらに、発泡粒子
の溶融温度以上の水蒸気を水蒸気室に導入し、成形体表
面を溶融硬化させて成形体の表面部にスキン層を形成し
ている。
[0004] In order to solve these problems, for example, JP-A-48-28060 and JP-A-52-47866.
Japanese Patent Application Laid-Open Publication No. H11-15064 proposes a method of forming a skin layer on the surface of a molded body by melting during molding. In these molding methods, a cavity mold and a core mold each having a steam chamber are used, and a foam molding mold having a large number of steam holes formed on a wall surface facing a cavity of each steam chamber is used. Is filled with foamed particles, steam having a temperature lower than the melting temperature of the foamed particles is introduced into a steam chamber, and the foamed particles are heated and fused together to form a molded body. It is introduced into a chamber, and the surface of the molded body is melt-hardened to form a skin layer on the surface of the molded body.

【0005】しかしながら、この方法の場合、発泡粒子
の溶融温度以上の水蒸気で加熱する際、蒸気孔付近が過
剰に溶融され、その結果、蒸気孔付近とそれ以外の箇所
のスキン層の各厚さなどが異なり、全体として不均一な
スキン層が形成される。また、発泡粒子同士の融着が先
に行われるため、個々の発泡粒子が結合して更なる自由
発泡が阻害され、発泡粒子間の空隙を十分に埋めること
が出来ない。また、成形体は、スキン層の厚さが増加す
るに伴い、部分的に空隙を発生するという問題があり、
空隙の少ない均一なスキン層を持った成形体は得られて
いなかった。
However, in the case of this method, when the foamed particles are heated with steam at a temperature higher than the melting temperature, the vicinity of the steam holes is excessively melted, and as a result, the thickness of the skin layer near the steam holes and other portions is reduced. And the like, and an uneven skin layer is formed as a whole. In addition, since the fusion of the foamed particles is performed first, the individual foamed particles are bonded to each other, and further free foaming is hindered, and the voids between the foamed particles cannot be sufficiently filled. In addition, the molded article has a problem that a gap is partially generated as the thickness of the skin layer increases,
A molded article having a uniform skin layer with few voids was not obtained.

【0006】特開平5−124126号公報には、発泡
粒子の融点以上に加熱した金型の成形表面に原料粒子を
接触溶融させ、その部分に溶融樹脂層を形成した後、こ
の溶融樹脂層を硬化させて連続した表面硬化層を型内発
泡成形過程で形成した発泡性樹脂成形体が提案されてい
る。
Japanese Patent Application Laid-Open No. 5-124126 discloses that raw material particles are contact-melted on a molding surface of a mold heated to a melting point of foamed particles or higher, and a molten resin layer is formed on that portion. There has been proposed a foamable resin molded article in which a continuous hardened surface layer is formed in an in-mold foam molding process.

【0007】しかしながら、上記の公報に記載の方法
は、過大なクラッキング充填によりスキン層を形成する
方法であり、従って、複雑な形状の成形体には対応でき
ず、箱形状の立上がり部などでは充填率が低くなって成
形体が収縮するという問題がある。
However, the method described in the above-mentioned publication is a method of forming a skin layer by excessive cracking filling, and therefore cannot cope with a molded article having a complicated shape. There is a problem that the ratio becomes low and the compact shrinks.

【0008】[0008]

【発明が解決しようとする課題】本発明は、上記実情に
鑑みなされたものであり、その目的は、複雑な形状であ
っても表面部に均一かつ高密度で硬いスキン層を備えた
収縮の少ない外観良好な成形体の製造方法を提供するこ
とにある。
SUMMARY OF THE INVENTION The present invention has been made in consideration of the above circumstances, and has as its object to reduce shrinkage by providing a uniform, high-density and hard skin layer on the surface even in a complicated shape. An object of the present invention is to provide a method for producing a molded article having a small appearance and good appearance.

【0009】[0009]

【課題を解決するための手段】すなわち、本発明の要旨
は、各々水蒸気室を備えたキャビ型およびコア型から成
る発泡成形用金型による成形体の製造方法に於いて、金
型のキャビティ内に発泡樹脂粒子を圧縮充填し、上記の
蒸気室の一方に水蒸気を導入して発泡樹脂粒子の融点以
上に金型を加熱すると共に当該金型と接触している発泡
樹脂粒子を溶融させてその表面にスキン層を形成し、キ
ャビティ内に充填した発泡樹脂粒子の面圧力が0.01
〜1.5kg/cm2Gの範囲に到達した際、発泡樹脂
粒子間の空気を排出させ、他方の蒸気室から発泡樹脂粒
子間に当該発泡樹脂の融点未満の水蒸気を導入して発泡
樹脂同士を加熱融着させることを特徴とする高密度のス
キン層を持つ成形体の製造方法に存する。
That is, the gist of the present invention is to provide a method of manufacturing a molded article by a foaming mold comprising a mold having a steam chamber and a core having a steam chamber. The foamed resin particles are compressed and filled, steam is introduced into one of the above-mentioned steam chambers to heat the mold to a temperature equal to or higher than the melting point of the foamed resin particles, and to melt the foamed resin particles that are in contact with the mold. A skin layer is formed on the surface, and the surface pressure of the foamed resin particles filled in the cavity is 0.01
When the pressure reaches the range of 1.5 kg / cm 2 G, the air between the foamed resin particles is exhausted, and steam having a melting point lower than the melting point of the foamed resin is introduced between the foamed resin particles from the other steam chamber to form the foamed resin particles. And a method for producing a molded article having a high-density skin layer, characterized by heating and fusing.

【0010】[0010]

【発明の実施の形態】以下、本発明を添付図に基づいて
詳細に説明する。図1は、本発明の方法に使用する発泡
成形用金型(以下、単に金型と略称する)の一例の概略
を示す断面図である。本発明においては、各々水蒸気室
を備えたキャビ型およびコア型から成る金型を使用す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to the accompanying drawings. FIG. 1 is a cross-sectional view schematically illustrating an example of a mold for foam molding (hereinafter simply referred to as a mold) used in the method of the present invention. In the present invention, molds each including a mold having a steam chamber and a mold having a core are used.

【0011】図1に示す金型は、凹状断面のキャビ型
(1)と、凸状断面のコア型(2)から成り、ボックス
状断面のキャビティ(3)を有する。そして、キャビテ
ィ(3)には、発泡粒子の圧縮充填タンク(4)から延
びる充填ノズル(5)の先端がキャビ型(1)を貫通し
て連通している。
The mold shown in FIG. 1 comprises a cavity mold (1) having a concave cross section and a core mold (2) having a convex cross section, and has a cavity (3) having a box cross section. The tip of a filling nozzle (5) extending from the compressed filling tank (4) for the foamed particles communicates with the cavity (3) through the mold (1).

【0012】キャビ型(1)は内部に蒸気室(1a)有
し、蒸気室(1a)のキャビティ(3)に面する壁面に
は、多数の蒸気孔(1b)が形成されている。そして、
蒸気室(1a)には、それぞれ開閉弁を有する水蒸気管
路(6)、真空管路(7)、冷却水管路(8)及びドレ
ン管路(9)が連通している。
The mold mold (1) has a steam chamber (1a) inside, and a large number of steam holes (1b) are formed in a wall surface of the steam chamber (1a) facing the cavity (3). And
A steam pipe (6), a vacuum pipe (7), a cooling water pipe (8), and a drain pipe (9) each having an on-off valve are connected to the steam chamber (1a).

【0013】一方、コア型(2)は、内部に第1蒸気室
(2a)と第2蒸気室(2b)とを有している。第1蒸
気室(2a)はキャビティ(3)側に位置し、第2蒸気
室(2b)は第1蒸気室(2a)の外側に位置する。各
蒸気室は相互に連通することなく完全に独立した構造を
備えている。そして、第1蒸気室(2a)には、それぞ
れ開閉弁を有する水蒸気管路(10)、冷却水管路(1
1)及びドレン管路(12)が連通している。また、第
2蒸気室(2b)には、それぞれ開閉弁を有する水蒸気
管路(13)、冷却水管路(14)及びドレン管路(1
5)が連通している。
On the other hand, the core type (2) has a first steam chamber (2a) and a second steam chamber (2b) inside. The first steam chamber (2a) is located on the cavity (3) side, and the second steam chamber (2b) is located outside the first steam chamber (2a). Each steam chamber has a completely independent structure without communication with each other. The first steam chamber (2a) has a steam pipe (10) and a cooling water pipe (1) each having an on-off valve.
1) and the drain line (12) are in communication. The second steam chamber (2b) has a steam pipe (13), a cooling water pipe (14), and a drain pipe (1) each having an on-off valve.
5) is in communication.

【0014】なお、上記に例示した金型においては、キ
ャビティ(3)内に充填した発泡樹脂粒子の表面にスキ
ン層を形成した後に発泡樹脂粒子間に当該発泡樹脂の融
点未満の水蒸気を導入して発泡樹脂同士を加熱融着させ
るために使用される蒸気孔(1b)が蒸気室(1a)の
キャビティ(3)に面する壁面に形成されているため、
上記のスキン層を形成するための水蒸気は、コア型
(2)の第1蒸気室(2a)と第2蒸気室(2b)に導
入されるが、発泡樹脂同士を加熱融着させるために使用
される蒸気孔が上記と逆方向の位置に形成されている金
型を使用する場合は、上記のスキン層を形成するための
水蒸気は、キャビ型(1)の蒸気室(1a)に導入され
る。本発明においては、上記の何れのタイプの金型をも
使用し得る。
In the above-described mold, after forming a skin layer on the surface of the foamed resin particles filled in the cavity (3), water vapor having a melting point lower than the melting point of the foamed resin is introduced between the foamed resin particles. Since the steam holes (1b) used to heat and fuse the foamed resins to each other are formed on the wall surface facing the cavity (3) of the steam chamber (1a),
The steam for forming the skin layer is introduced into the first steam chamber (2a) and the second steam chamber (2b) of the core mold (2), and is used to heat and fuse the foamed resins to each other. When using a mold in which the steam holes to be formed are formed in positions opposite to the above, the steam for forming the skin layer is introduced into the steam chamber (1a) of the mold type (1). You. In the present invention, any of the molds described above can be used.

【0015】本発明で使用される発泡粒子としては、ポ
リスチレン系樹脂粒子、ポリエチレン系樹脂粒子、ポリ
プロピレン系樹脂粒子などが挙げられる。これらの発泡
粒子は、圧縮空気により圧縮充填タンク(4)内に圧縮
充填された後、金型のキャビティ(3)内に均一に圧縮
充填される。
The expanded particles used in the present invention include polystyrene resin particles, polyethylene resin particles, and polypropylene resin particles. These foamed particles are compressed and filled into the compression filling tank (4) with compressed air, and then uniformly compressed into the mold cavity (3).

【0016】先ず、本発明においては、金型のキャビテ
ィ(3)内に発泡樹脂粒子を圧縮充填し、上記の蒸気室
の一方に水蒸気を導入して発泡樹脂粒子の融点以上に金
型を加熱すると共に当該金型と接触している発泡樹脂粒
子を溶融させてその表面にスキン層を形成する。
First, in the present invention, foamed resin particles are compression-filled into a cavity (3) of a mold, and steam is introduced into one of the above-mentioned steam chambers to heat the mold to a temperature equal to or higher than the melting point of the foamed resin particles. At the same time, the foamed resin particles in contact with the mold are melted to form a skin layer on the surface.

【0017】具体的には、水蒸気管路(10)、(1
3)の弁およびドレン管路(12)、(15)の弁を開
放し、第1蒸気室(2a)及び第2蒸気室(2b)に高
温の水蒸気を導入して金型を予熱しながら密閉し、圧縮
充填タンク(4)内に収容された発泡粒子を充填ノズル
(5)によりキャビティ(3)内に圧縮充填する。そし
て、第1蒸気室(2a)及び第2蒸気室(2b)の金型
温度が一定温度以上に到達したとき、ドレン管路(1
2)及び(15)の弁を閉じ、キャビティ(3)内の発
泡粒子と接触する第1蒸気室(2a)側の金型温度を発
泡粒子の融点以上まで昇温する。
Specifically, the steam lines (10), (1)
The valve of 3) and the valves of the drain lines (12) and (15) are opened, and high-temperature steam is introduced into the first steam chamber (2a) and the second steam chamber (2b) while preheating the mold. The hermetically sealed foamed particles contained in the compression filling tank (4) are compressed and filled into the cavity (3) by the filling nozzle (5). When the mold temperature of the first steam chamber (2a) and the second steam chamber (2b) reaches a certain temperature or higher, the drain pipe (1
The valves of 2) and (15) are closed, and the mold temperature on the side of the first steam chamber (2a) in contact with the foamed particles in the cavity (3) is raised to the melting point of the foamed particles or more.

【0018】本発明の好ましい態様においては、発泡粒
子の上記の充填の際、目標とする成形体の強度や品質を
確保するため、スキン層の厚さ、スキン層の密度、スキ
ン層以外の成形体の密度などを事前に設定しておき、下
記(I)の数式により求めた発泡粒子の圧縮率を使用す
る。ここで、スキン層の密度としては、使用する発泡粒
子のソリッド状態の密度を使用する。因みに、ポリスチ
レン系発泡粒子のソリッド状態の密度は950〜100
0kg/m3、ポリプロピレン発泡粒子のソリッド状態
の密度は850〜900kg/m3である。
In a preferred embodiment of the present invention, the thickness of the skin layer, the density of the skin layer, and the molding other than the skin layer are performed at the time of the above-mentioned filling of the foamed particles in order to ensure the strength and quality of the target molded body. The density of the body is set in advance, and the compression ratio of the foamed particles obtained by the following mathematical expression (I) is used. Here, the density of the solid state of the foamed particles to be used is used as the density of the skin layer. Incidentally, the density of the solid state of the expanded polystyrene particles is 950 to 100.
0 kg / m 3, the density of the solid state of the polypropylene expanded particles are 850~900kg / m 3.

【0019】本発明においては、発泡粒子の圧縮率は、
通常3〜70%、好ましくは10〜65%とされる。圧
縮率が3%未満の場合は、発泡粒子の充填量が不足し、
スキン層形成が出来にくく、成形体が収縮する。また、
圧縮率が70%を超える場合は、スキン層を厚くするこ
とが可能となるが加熱溶融時間が長くなり、さらに、圧
縮充填時の圧縮空気の使用量が増加して製造コストが高
くなる。
In the present invention, the compression ratio of the expanded particles is
Usually, it is 3 to 70%, preferably 10 to 65%. If the compression ratio is less than 3%, the filling amount of the expanded particles is insufficient,
It is difficult to form a skin layer and the molded product shrinks. Also,
When the compression ratio exceeds 70%, the skin layer can be made thicker, but the heating and melting time becomes longer, and the amount of compressed air used during compression filling increases, resulting in higher production costs.

【0020】[0020]

【数2】 C=(1−ρ1/((ρ2×t2+ρ3×t3)/t1))×100 (I) C :圧縮率 (%) ρ1:充填前の発泡樹脂粒子密度 (kg/m3 ) ρ2:スキン層部の密度 (kg/m3) ρ3:スキン層部以外の密度 (kg/m3) t1:成形体肉厚 (mm) t2:スキン層部の厚さ (mm) t3:スキン層部以外の厚さ (mm)C = (1-ρ)1/ ((ΡTwo× tTwo+ ΡThree× tThree) / T1)) × 100 (I) C: Compression rate (%) ρ1: Density of expanded resin particles before filling (kg / mThree ) ΡTwo: Density of skin layer (kg / mThree) ΡThree: Density other than skin layer (kg / mThree) T1: Molded body thickness (mm) tTwo: Thickness of skin layer (mm) tThree: Thickness other than skin layer (mm)

【0021】ところで、金型内に圧縮充填された発泡粒
子は、大気圧以上の面圧力を有しているが、スキン層の
形成に伴って発泡粒子の体積が減少するため、大気圧以
上であった面圧力は、スキン層の形成に伴って低下す
る。
The foamed particles compressed and filled in the mold have a surface pressure higher than the atmospheric pressure. However, the volume of the foamed particles decreases with the formation of the skin layer. The existing surface pressure decreases with the formation of the skin layer.

【0022】そこで、本発明においては、上記の操作に
引き続き、キャビティ(3)内に充填した発泡樹脂粒子
の面圧力が0.01〜1.5kg/cm2Gの範囲に到
達した際、内部粒子の融着がより良好な成形体を得るた
めに発泡樹脂粒子間の空気を排出させ、発泡樹脂粒子間
に当該発泡樹脂の融点未満の水蒸気を導入して発泡樹脂
同士を加熱融着させる。
Therefore, in the present invention, when the surface pressure of the foamed resin particles filled in the cavity (3) reaches the range of 0.01 to 1.5 kg / cm 2 G, the internal In order to obtain a molded body with better fusion of the particles, air between the foamed resin particles is discharged, and steam having a melting point lower than the melting point of the foamed resin is introduced between the foamed resin particles to heat and fuse the foamed resins to each other.

【0023】具体的には、キャビティ(3)内に充填さ
れた発泡粒子の面圧力がスキン層の形成に伴って一定の
値から低下して上記の特定値に到達した際、真空管路
(7)弁を開放し、ドレン管路(9)弁を閉じ、蒸気室
(1a)及びキャビティ(3)内を真空排気した後、真
空管路(7)弁を閉じ、型内の発泡粒子の融着に必要な
温度の水蒸気を水蒸気管路(6)より導入して加熱す
る。水蒸気は、水蒸気管路(6)より蒸気室(1a)を
通り、蒸気孔(1b)を介してキャビティ(3)内に流
入し、発泡粒子を加熱する。この際、水蒸気は、成形金
型を加熱する熱媒としても作用する。すなわち、水蒸気
加熱によれば、その大きな熱容量を利用し、短時間で均
一な温度を効率よく得ることが出来る。
More specifically, when the surface pressure of the foamed particles filled in the cavity (3) decreases from a certain value with the formation of the skin layer and reaches the above-mentioned specific value, the vacuum line (7) ) Open the valve, close the drain line (9) valve, evacuate the steam chamber (1a) and the cavity (3), then close the vacuum line (7) valve, and fuse the expanded particles in the mold. Is introduced through a steam line (6) and heated. The steam passes through the steam chamber (1a) from the steam line (6), flows into the cavity (3) through the steam hole (1b), and heats the foamed particles. At this time, the water vapor also acts as a heat medium for heating the molding die. That is, according to the steam heating, a uniform temperature can be efficiently obtained in a short time by utilizing the large heat capacity.

【0024】前記の面圧力が0.01kg/cm2G未
満の場合は、水蒸気で発泡粒子を加熱融着した際、発泡
粒子が過大に発泡して充填密度が低下するため、発泡力
が減少し、融着不良、成形体の収縮、スキン層部と成形
体部の剥離現象が起こり、良好な成形体が得られない。
面圧力が1.5kg/cm2Gを超える場合は、発泡粒
子を融着加熱するために導入した水蒸気が発泡粒子の内
部にまで浸透しないため、加熱不足による発泡粒子の融
着不良が起こり、良好な成形体が得られない。
When the surface pressure is less than 0.01 kg / cm 2 G, when the foamed particles are heated and fused with water vapor, the foamed particles are excessively foamed and the packing density is reduced, so that the foaming power is reduced. However, poor fusion occurs, shrinkage of the molded body, and a peeling phenomenon between the skin layer portion and the molded body portion occur, and a good molded body cannot be obtained.
If the surface pressure exceeds 1.5 kg / cm 2 G, the steam introduced for fusing and heating the foamed particles does not penetrate into the foamed particles. Good molded products cannot be obtained.

【0025】ついで、本発明においては、水蒸気管路
(6)、(10)及び(13)の弁を閉じ、ドレン管路
(9)、(12)及び(15)の弁を開放し、冷却水管
路(8)、(11)及び(14)の弁も開放する。その
後、蒸気室(1a)、第1蒸気室(2a)及び第2蒸気
室(2b)に冷却水を導入して金型を冷却した後、成形
体を取り出す。
Next, in the present invention, the valves of the steam lines (6), (10) and (13) are closed, the valves of the drain lines (9), (12) and (15) are opened, and cooling is performed. The valves of the water lines (8), (11) and (14) are also opened. Then, after cooling water is introduced into the steam chamber (1a), the first steam chamber (2a), and the second steam chamber (2b) to cool the mold, the molded body is taken out.

【0026】[0026]

【実施例】以下、本発明を実施例により更に詳細に説明
するが、本発明はその要旨を超えない限り、以下の実施
例に限定されるものではない。なお、実施例において
は、図1に示す装置を使用し、縦200mm、横400
mm、高さ250mm及び肉厚20mmの箱状成形体の
金型を使用した。なお、以下の各例において、成形体製
造における圧縮率、成形体の融着度および収縮は、次の
様にして求めた。
EXAMPLES Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist. In the embodiment, the apparatus shown in FIG.
mm, a height of 250 mm and a wall thickness of 20 mm were used. In each of the following examples, the compression ratio, the degree of fusion of the molded body, and the shrinkage in the production of the molded body were determined as follows.

【0027】<圧縮率>圧縮率は、(1−発泡粒子密度
/成形体密度) ×100%の式で求めた。
<Compression Ratio> The compression ratio was determined by the formula (1−expanded particle density / molded product density) × 100%.

【0028】<融着度>融着度は、成形体を破断して発
泡粒子の界面以外で割れた面積の破断全体の面積に対す
る割合で評価した。
<Degree of fusion> The degree of fusion was evaluated by the ratio of the area of the molded article which was broken at the interface other than the interface of the foamed particles to the area of the entire fracture.

【0029】<収縮>収縮は、成形体の寸法が5/10
0以上減少した場合を「有」、5/100未満減少した
場合を「無」とした。
<Shrinkage> Shrinkage occurs when the size of the molded article is 5/10.
The case where it decreased by 0 or more was judged as “present”, and the case where it decreased less than 5/100 was judged as “absent”.

【0030】実施例1 スキン層部の厚さが0.5mm、スキン層密度が850
kg/m3、スキン層以外の密度が50kg/m3、成形
体の全体の肉厚が20mmの成形体を製造するため、前
記(1)の数式より圧縮率約54%を算出した。
Example 1 The thickness of the skin layer was 0.5 mm and the density of the skin layer was 850.
kg / m 3, density of 50 kg / m 3 other than the skin layer, since the thickness of the entire shaped body to produce a molded body of 20 mm, was calculated about 54% compression rate than formula (1).

【0031】密度32kg/m3のポリプロピレン発泡
粒子を圧縮充填タンク(4)に充填し、ついで、水蒸気
管路(10)、(13)の弁およびドレン管路(1
2)、(15)の弁を開放し、第1蒸気室(2a)に1
75℃、第2蒸気室(2b)に150℃の水蒸気を導入
して金型を予熱しながら密閉した。
The compression-filled tank (4) is filled with expanded polypropylene particles having a density of 32 kg / m 3 , and then the valves of the steam lines (10) and (13) and the drain line (1) are filled.
2) Open the valves of (15) and put 1 in the first steam chamber (2a).
Steam was introduced into the second steam chamber (2b) at 75 ° C., and the mold was sealed while preheating the mold.

【0032】キャビティ(3)内に圧縮充填タンク
(4)から充填ノズル(5)により発泡粒子を圧縮充填
した。第1蒸気室(2a)及び第2蒸気室(2b)の金
型温度が100℃以上に到達したとき、ドレン管路(1
2)及び(15)の弁を閉じた。その結果、キャビティ
(3)内の発泡粒子と接触する第1蒸気室(2a)側の
金型温度は、170℃まで急速に昇温し安定した。
The foaming particles were compression-filled into the cavity (3) from the compression-filling tank (4) by the filling nozzle (5). When the mold temperature of the first steam chamber (2a) and the second steam chamber (2b) reaches 100 ° C. or more, the drain pipe (1
The valves of 2) and (15) were closed. As a result, the mold temperature on the side of the first steam chamber (2a) in contact with the foamed particles in the cavity (3) rapidly rose to 170 ° C. and was stabilized.

【0033】このとき、キャビティ(3)内に充填され
た発泡粒子の面圧力は、1.6kg/cm2Gを示し
た。面圧力は、図2に示す様に低下した。面圧力が0.
5kg/cm2Gに到達したとき、真空管路(7)弁を
開放し、ドレン管路(9)弁を閉じ、蒸気室(1a)及
びキャビティ(3)内を真空排気した後、真空管路
(7)弁を閉じ、発泡粒子の融点未満の水蒸気を水蒸気
管路(6)より導入して加熱した。発泡粒子は、水蒸気
管路(6)より蒸気室(1a)を通り、蒸気孔(1b)
を介してキャビティ(3)内に流入した水蒸気により加
熱された。蒸気温度は150℃であり、保持時間は20
秒であった。
At this time, the surface pressure of the expanded particles filled in the cavity (3) was 1.6 kg / cm 2 G. The surface pressure decreased as shown in FIG. Surface pressure is 0.
When the pressure reaches 5 kg / cm 2 G, the vacuum line (7) valve is opened, the drain line (9) valve is closed, and the inside of the steam chamber (1a) and the cavity (3) is evacuated. 7) The valve was closed and steam having a melting point lower than the melting point of the foamed particles was introduced from the steam line (6) and heated. The expanded particles pass through the steam chamber (1a) from the steam line (6), and pass through the steam holes (1b).
And heated by the steam flowing into the cavity (3). The steam temperature is 150 ° C. and the holding time is 20
Seconds.

【0034】ついで、水蒸気管路(6)、(10)及び
(13)の弁を閉め、ドレン管路(9)、(12)及び
(15)の弁を開放し、冷却水管路(8)、(11)及
び(14)の弁も開放した。蒸気室(1a)、第1蒸気
室(2a)及び第2蒸気室(2b)に冷却水を導入し、
金型を40℃まで冷却した。成形体を金型から取り出し
た。結果を表1に示す。
Next, the valves of the steam lines (6), (10) and (13) are closed, the valves of the drain lines (9), (12) and (15) are opened, and the cooling water line (8) is opened. , (11) and (14) were also opened. Introducing cooling water into the steam chamber (1a), the first steam chamber (2a) and the second steam chamber (2b);
The mold was cooled to 40 ° C. The compact was removed from the mold. Table 1 shows the results.

【0035】実施例2 実施例1において、表1に示す条件を採用し、キャビテ
ィ(3)内に48kg/m3の発泡ポリプロピレン発泡
粒子を圧縮充填し、面圧力が図2に示す様に0.4kg
/cm2Gになったとき、真空排気した以外は、実施例
1と同一条件で成形を行なった。結果を表1に示す。
Example 2 In Example 1, the conditions shown in Table 1 were adopted, and 48 kg / m 3 of expanded polypropylene expanded particles were compression-filled into the cavity (3), and the surface pressure was reduced to 0 as shown in FIG. 0.4 kg
/ Cm 2 G, molding was performed under the same conditions as in Example 1 except that evacuation was performed. Table 1 shows the results.

【0036】比較例1 実施例1において、発泡粒子の面圧力が0kg/cm2
Gまで低下したとき、真空排気した以外は、実施例1と
同一条件で成形を行なった。結果を表1に示す。
Comparative Example 1 In Example 1, the surface pressure of the foamed particles was 0 kg / cm 2.
Molding was performed under the same conditions as in Example 1 except that the gas was evacuated when the temperature decreased to G. Table 1 shows the results.

【0037】比較例2 実施例1において、発泡粒子の面圧力が1.6kg/c
2Gのとき、真空排気した以外は、実施例1と同一条
件で成形を行なった。結果を表1に示す。
Comparative Example 2 In Example 1, the expanded particles had a surface pressure of 1.6 kg / c.
Molding was carried out under the same conditions as in Example 1 except that evacuation was performed at m 2 G. Table 1 shows the results.

【0038】比較例3 実施例1において、金型を20mm開けたクラッキング
充填に変更し、箱状の成形体の底部に相当する部分の圧
縮率が50%、側面立上部の平均圧縮率が7.4%とな
る条件を採用した以外は、実施例1と同一条件で成形を
行なった。結果を表1に示す。
COMPARATIVE EXAMPLE 3 In Example 1, the mold was changed to cracking filling in which the mold was opened by 20 mm, and the compression ratio of the portion corresponding to the bottom of the box-shaped molded product was 50%, and the average compression ratio of the ridge at the side was 7%. The molding was carried out under the same conditions as in Example 1 except that the condition of 0.4% was adopted. Table 1 shows the results.

【0039】[0039]

【表1】 比較例3の左欄:箱状成形体の底部 比較例3の右欄:箱状成形体の底部以外の側面立上部 −:測定不可[Table 1] Left column of Comparative Example 3: Bottom of box-shaped molded product Right column of Comparative Example 3: Upside of side surface other than bottom of box-shaped molded product-: Measurement not possible

【0040】実施例1及び2で得られた成形体は、均一
なスキン層および良好な外観を有し、収縮も無かった。
比較例1〜3で得られた成形体は、融着が劣り外観は不
良であった。
The molded articles obtained in Examples 1 and 2 had a uniform skin layer, a good appearance, and no shrinkage.
The molded articles obtained in Comparative Examples 1 to 3 had poor fusion and poor appearance.

【0041】[0041]

【発明の効果】以上説明した本発明の製造方法によれ
ば、成形体の表面部に均一かつ高密度で硬いスキン層を
備えた収縮の少ない良好な成形体が得られ、樹脂シート
との同時成形が不要で安価に成形体を製造することが出
来る。
According to the manufacturing method of the present invention described above, a good molded article having a uniform, high-density and hard skin layer on the surface of the molded article and having a small shrinkage can be obtained. Molding is unnecessary and a molded body can be manufactured at low cost.

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

【図1】本発明における成形体を製造する金型の一例の
概略を示す断面図である。
FIG. 1 is a cross-sectional view schematically showing an example of a mold for producing a molded article according to the present invention.

【図2】実施例1及び2における加熱時間−面圧力関係
の曲線である。
FIG. 2 is a curve showing a relationship between heating time and surface pressure in Examples 1 and 2.

【符号の説明】[Explanation of symbols]

1 :キャビ型 1a :蒸気室 1b :蒸気孔 2 :コア型 2a :第1蒸気室 2b :第2蒸気室 3 :キャビティ 4 :圧縮充填タンク 5 :充填ノズル 6、10、13 :水蒸気管路 7 :真空管路 8、11、14 :冷却水管路 9、12、15 :ドレン管路 1: Cabinet type 1a: Steam chamber 1b: Steam hole 2: Core type 2a: First steam chamber 2b: Second steam chamber 3: Cavity 4: Compression filling tank 5: Filling nozzle 6, 10, 13: Steam line 7 : Vacuum lines 8, 11, 14: Cooling water lines 9, 12, 15: Drain lines

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29K 25:00 105:04 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code Agency reference number FI Technical display location B29K 25:00 105: 04

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 各々水蒸気室を備えたキャビ型およびコ
ア型から成る発泡成形用金型による成形体の製造方法に
於いて、金型のキャビティ内に発泡樹脂粒子を圧縮充填
し、上記の蒸気室の一方に水蒸気を導入して発泡樹脂粒
子の融点以上に金型を加熱すると共に当該金型と接触し
ている発泡樹脂粒子を溶融させてその表面にスキン層を
形成し、キャビティ内に充填した発泡樹脂粒子の面圧力
が0.01〜1.5kg/cm2Gの範囲に到達した
際、発泡樹脂粒子間の空気を排出させ、他方の蒸気室か
ら発泡樹脂粒子間に当該発泡樹脂の融点未満の水蒸気を
導入して発泡樹脂同士を加熱融着させることを特徴とす
る高密度のスキン層を持つ成形体の製造方法。
In a method for producing a molded article by a foaming mold comprising a mold and a core each having a steam chamber, foamed resin particles are compression-filled into a cavity of the mold, and the steam is filled. Water vapor is introduced into one of the chambers to heat the mold above the melting point of the foamed resin particles and to melt the foamed resin particles in contact with the mold to form a skin layer on the surface and fill the cavity. When the surface pressure of the foamed resin particles reaches a range of 0.01 to 1.5 kg / cm 2 G, the air between the foamed resin particles is discharged, and the foamed resin particles are discharged from the other steam chamber to the space between the foamed resin particles. A method for producing a molded article having a high-density skin layer, comprising introducing steam having a melting point lower than the melting point to heat and fuse the foamed resins to each other.
【請求項2】 下記(I)の数式で示される圧縮率が3
〜70%の範囲になる様に発泡樹脂粒子の充填を行う請
求項1に記載の製造方法。 【数1】 C=(1−ρ1/((ρ2×t2+ρ3×t3)/t1))×100 (I) C :圧縮率 (%) ρ1:充填前の発泡樹脂粒子密度 (kg/m3 ) ρ2:スキン層部の密度 (kg/m3) ρ3:スキン層部以外の密度 (kg/m3) t1:成形体肉厚 (mm) t2:スキン層部の厚さ (mm) t3:スキン層部以外の厚さ (mm)
2. The compression ratio represented by the following equation (I) is 3
The filling of foamed resin particles to be in the range of ~ 70%
The method according to claim 1. C = (1-ρ)1/ ((ΡTwo× tTwo+ ΡThree× tThree) / T1)) × 100 (I) C: Compression rate (%) ρ1: Density of expanded resin particles before filling (kg / mThree ) ΡTwo: Density of skin layer (kg / mThree) ΡThree: Density other than skin layer (kg / mThree) T1: Molded body thickness (mm) tTwo: Thickness of skin layer (mm) tThree: Thickness other than skin layer (mm)
【請求項3】 発泡樹脂粒子がポリスチレン系樹脂粒
子、ポリエチレン系樹脂粒子およびポリプロピレン系樹
脂粒子の群より選ばれた少なくとも1種である請求項1
又は2に記載の製造方法。
3. The foamed resin particles are at least one selected from the group consisting of polystyrene resin particles, polyethylene resin particles and polypropylene resin particles.
Or the production method according to 2.
JP9113338A 1996-04-25 1997-04-15 Manufacture of molding having high density skin layer Pending JPH1034753A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9113338A JPH1034753A (en) 1996-04-25 1997-04-15 Manufacture of molding having high density skin layer

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP8-129059 1996-04-25
JP12905996 1996-04-25
JP9113338A JPH1034753A (en) 1996-04-25 1997-04-15 Manufacture of molding having high density skin layer

Publications (1)

Publication Number Publication Date
JPH1034753A true JPH1034753A (en) 1998-02-10

Family

ID=26452333

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9113338A Pending JPH1034753A (en) 1996-04-25 1997-04-15 Manufacture of molding having high density skin layer

Country Status (1)

Country Link
JP (1) JPH1034753A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005105404A1 (en) * 2004-05-03 2005-11-10 Polma Co., Ltd. Molding method and apparatus for expandable polymer resin
JP2006319464A (en) * 2005-05-10 2006-11-24 Pioneer Electronic Corp Manufacturing method for diaphragm used for speaker device
KR101134489B1 (en) * 2010-01-22 2012-04-13 (주)코모텍 Manufacturing apparatus of foam-molding product and manufacturing method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005105404A1 (en) * 2004-05-03 2005-11-10 Polma Co., Ltd. Molding method and apparatus for expandable polymer resin
JP2006319464A (en) * 2005-05-10 2006-11-24 Pioneer Electronic Corp Manufacturing method for diaphragm used for speaker device
KR101134489B1 (en) * 2010-01-22 2012-04-13 (주)코모텍 Manufacturing apparatus of foam-molding product and manufacturing method thereof

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