JPH11138575A - Manufacture of molding with high density skin layer - Google Patents

Manufacture of molding with high density skin layer

Info

Publication number
JPH11138575A
JPH11138575A JP9322220A JP32222097A JPH11138575A JP H11138575 A JPH11138575 A JP H11138575A JP 9322220 A JP9322220 A JP 9322220A JP 32222097 A JP32222097 A JP 32222097A JP H11138575 A JPH11138575 A JP H11138575A
Authority
JP
Japan
Prior art keywords
skin layer
particles
mold
steam
density
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.)
Granted
Application number
JP9322220A
Other languages
Japanese (ja)
Other versions
JP3859330B2 (en
Inventor
Masaaki Yokoyama
正明 横山
Toshihiro Goto
敏宏 後藤
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 JP32222097A priority Critical patent/JP3859330B2/en
Publication of JPH11138575A publication Critical patent/JPH11138575A/en
Application granted granted Critical
Publication of JP3859330B2 publication Critical patent/JP3859330B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a qualitatively uniform and hard skin layer which is almost free from shrinkage by filling a mold with foamable resin particles under compression so that the particles show a specific compressibility, then heating the particles to a temperature higher than a melt point to form the skin layer on the surface of a molding which comes into contact with the mold, and removing an air from between the particles when the area pressure of the particles is within a specific range to thermally fuse the textures of the resin mutually. SOLUTION: Foaming particles contained in a compression charging tank 4 are charged into the cavity 3 of a mold which is preheated and hermetically sealed within the range of 3-70% of the compressibility C shown by formula C=(1-ρ1/((ρ2×2t2+ρ3×t3)/(t1))×100 (wherein, C is compressibility %; ρ1 is the density kg/m<3> of foamable resin particles before charging; ρ2 is the density kg/m<3> of a skin layer part; ρ3 is the density kg/m<3> of a part other than the skin layer part; t1 is the wall thickness mm of a molding; t2 is the thickness mm of the skin layer part; and t3 is the thickness mm of part other than the skin layer). The halves of the mold are heated at a temperature level above the melts point of the foamable particles. When the area pressure of the foamable particles in the cavity 3 is down to 0.01-1.5 kg/cm<2> G, the foamable particles are mutually fused together after exhausting the air. Thus it is possible to form a qualitatively uniform and high density hard skin layer over the entire face of a molding and consequently, obtain the molding almost free from shrinkage.

Description

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

【0001】[0001]

【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,成形体の表面部の略全面
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
上記の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 producing a molded article having a high-density skin layer, and more particularly, to a method for producing a molded article having a uniform, high-density and hard skin layer over substantially the entire surface of the molded article. The present invention relates to a method for manufacturing a molded article.

【0002】[0002]

【従来技術】各々水蒸気室を備えたキャビ型及びコア型
からなる発泡成形用金型内に発泡樹脂粒子(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かつ断熱性及び緩衝性に富み,
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。しかしながら,
成形体の表面には粒子間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
間隙に汚れが入ると共に割れ易く,また,成型品表面部
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,容器内部及び外部を
コーティングする方法や樹脂シートと一体成形する方法
を採用せざるを得ず,製造の工数増加や成形サイクルの
延長に伴って得られる成形体のコストが高いと言う問題
がある。
2. Description of the Related Art Molded articles produced by filling foamed resin particles (hereinafter referred to as "foamed particles") in a foaming mold composed of a mold cavity and a core mold each having a steam chamber and heat-sealing the molded articles are independent. It has a bubble structure and is rich in heat insulation and cushioning,
Moreover, it has the feature of being light, and is used for cushioning materials, heat insulating materials, heat insulating containers, and functional members. However,
Since there is a slight gap between particles on the surface of the compact,
When used repeatedly in applications such as containers, there is a problem that dirt enters the gaps between the particles and is easily broken, and the surface of the molded product is soft and easily scratched. For this reason, in the conventional manufacturing method, a method of coating the inside and outside of the container and a method of integrally molding with the resin sheet have to be adopted, and the molded body obtained by increasing the number of manufacturing steps and extending the molding cycle is required. There is a problem that the cost is high.

【0003】これらの問題を解決するために,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,例えば,特開昭48−28060号公報,特開昭
52−47866号公報等で提案されている。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及
びコア型からなり,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,金型内に発泡粒子を充填し,発泡粒子の溶融点未満
の水蒸気を水蒸気室に導入して加熱融着させた後,更
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。
[0003] In order to solve these problems, a method of forming a skin layer on the surface of a molded article by melting during molding is disclosed in, for example, JP-A-48-28060 and JP-A-52-47866. It has been proposed in gazettes and the like. In these molding methods, a mold for foam molding is used which comprises a mold cavity and a core mold each having a steam chamber, and has a large number of steam holes formed on a wall surface facing a cavity of each steam chamber. After filling the foamed particles in the mold, introducing steam having a melting point lower than the melting point of the foamed particles into the steam chamber and performing heat fusion, further introducing steam having a melting temperature equal to or higher than the melting point of the foamed particles into the steam chamber, The surface is melt-hardened to form a skin layer on the surface of the molded body.

【0004】しかしながら,この方法の場合,蒸気孔付
近は過剰に溶融され,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,発泡粒子の融着が先
に行われるため,各々の個々の発泡粒子が結合して更な
る自由発泡が阻害され,空間を充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,部分的に空隙が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, the vicinity of the steam hole is excessively melted, and as a result, the thickness of the skin layer in the vicinity of the steam hole and other portions is different, and a non-uniform skin layer is formed as a whole. You. Further, since the fusion of the foamed particles is performed first, the individual foamed particles are combined to inhibit further free foaming, so that the space cannot be sufficiently filled. Further, the molded article has a problem that voids are partially generated as the thickness of the skin layer increases, and a molded article having a uniform skin layer with few voids has not been obtained.

【0005】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
泡成形課程で形成した発泡樹脂成形体が提案されてい
る。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出来ず,箱形
状の立ち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。
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 foamed resin molded article in which a continuous hardened surface layer is formed in an in-mold foam molding process. However, the method described in the above publication is a method in which a skin layer is formed by excessive cracking filling, and therefore cannot be applied to a molded article having a complicated shape, and the filling rate is low in a box-shaped rising portion or the like. As a result, the molded article shrinks.

【0006】一般に金型に圧縮充填された発泡粒子は,
大気圧以上の面圧力(反発力)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し,面圧力はス
キン層の形成に伴って低下する。面圧力が特定値未満に
あるときは,水蒸気で加熱融着すると,発泡粒子が過大
に発泡し充填前の密度以下となり,発泡力が減少して融
着不良や成形体の収縮が発生し,良好な成形体が得られ
ない。一方,面圧力が特定値を越えるときは,発泡粒子
を溶融加熱するために導入した水蒸気が発泡粒子の内部
まで浸透せず,加熱不足による融着不良となって良好な
成形体が得られない。
[0006] In general, foamed particles compressed and filled in a mold are:
Although it has a surface pressure (repulsive force) higher than the atmospheric pressure, the volume of the foamed particles decreases with the formation of the skin layer, and the surface pressure decreases with the formation of the skin layer. When the surface pressure is less than the specified value, when heated and fused with water vapor, the foamed particles are excessively foamed and become less than the density before filling, the foaming power is reduced, and defective fusion or shrinkage of the molded body occurs. Good molded products cannot be obtained. On the other hand, when the surface pressure exceeds a specific value, the steam introduced for melting and heating the foamed particles does not penetrate into the interior of the foamed particles, resulting in poor fusion due to insufficient heating, and a good molded body cannot be obtained. .

【0007】[0007]

【解決しようとする課題】本発明は,上記事情に鑑みな
されたものであり,複雑な形状であっても成形体の表面
部の略全面に均一かつ高密度で硬いスキン層を備え,収
縮の少ない外観良好な成形体を得ることが出来る,高密
度のスキン層を持つ成形体の製造方法を提供しようとす
るものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and has a uniform, high-density, hard skin layer on almost the entire surface of a molded body even if it has a complicated shape, and has a shrinkage of shrinkage. An object of the present invention is to provide a method for producing a molded article having a high-density skin layer, which can obtain a molded article with a small appearance and good appearance.

【0008】[0008]

【課題の解決手段】即ち,本発明の要旨は,各々水蒸気
室を備えたキャビ型及びコア型からなる発泡成形用金型
内に発泡樹脂粒子を充填し加熱融着させる成形体の製造
方法に於いて,金型内に発泡樹脂粒子を圧縮充填し,上
記の両方の蒸気室とも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成形体表面にスキン層を
形成し,金型に充填した発泡樹脂粒子の面圧力を検出
し,その面圧力が0.01〜1.5kg/cm2 Gの範
囲にあるとき,金型内に残存する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 for producing a molded article in which foamed resin particles are filled into a mold for foaming molding comprising a mold cavity and a core mold each having a steam chamber and heated and fused. In this case, foamed resin particles are compressed and filled in a mold, steam is introduced into both of the steam chambers to heat the mold to a temperature higher than the melting point of the foamed resin particles, and the foamed resin in contact with the mold. A skin layer is formed on the surface of the molded body by melting the particles, and the surface pressure of the foamed resin particles filled in the mold is detected. When the surface pressure is in the range of 0.01 to 1.5 kg / cm 2 G Discharging air between the foamed resin particles remaining in the mold, introducing steam between the foamed resin particles having a melting point lower than the melting point of the foamed resin, and heating and fusing the foamed resins to each other. The present invention relates to a method for producing a molded article having a skin layer.

【0009】[0009]

【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
を備えたキャビ型及びコア型からなる金型を使用する。
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 sectional view schematically showing 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, a mold including a mold having a steam chamber and a mold having a core is used.

【0010】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)からなり,ボックス
状断面のキャビティ(3)を有する。そして,キャビ型
(1)とコア型(2)は発泡粒子は通過出来ないが気体
は通過出来る隙間(20)を持った状態で勘合してい
る。また,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 section and a core mold (2) having a convex section, and has a cavity (3) having a box-shaped section. The mold (1) and the core (2) are fitted together with a gap (20) through which the foamed particles cannot pass but a gas can pass. Further, 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).

【0011】キャビ型(1)は内部に第一蒸気室(1
a)と第二蒸気室(1b)とを有している。第二蒸気室
(1b)はキャビティ(3)側に位置し,第一蒸気室
(1a)は第二蒸気室(1b)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,第一蒸気室(1a)には,それぞれ
の開閉弁を有する水蒸気管路(8),冷却水管路
(6),真空管路(7)及びドレン管路(19)が連通
している。
The mold (1) has a first steam chamber (1) inside.
a) and a second steam chamber (1b). The second steam chamber (1b) is located on the cavity (3) side, and the first steam chamber (1a) is located outside the second steam chamber (1b). Each steam chamber has a completely independent structure without communication with each other. The first steam chamber (1a) communicates with a steam pipe (8), a cooling water pipe (6), a vacuum pipe (7), and a drain pipe (19) each having an on-off valve.

【0012】また,第一蒸気室(1a)は,隙間(2
0)を介してキャビティ(3)に連通する小室(22)
と蒸気孔(1c)にて連通している。第二蒸気室(1
b)には,それぞれの開閉弁を有する水蒸気管路(1
0),冷却水管路(9)及びドレン管路(18)が連通
している。
The first steam chamber (1a) is provided with a gap (2
Small chamber (22) communicating with cavity (3) via 0)
With the steam hole (1c). Second steam chamber (1
b) has a steam line (1
0), the cooling water pipe (9) and the drain pipe (18) communicate with each other.

【0013】一方,コア型(2)は内部に第一蒸気室
(2a)と第二蒸気室(2b)とを有している。第二蒸
気室(2b)はキャビティ(3)側に位置し,第一蒸気
室(2a)は第二蒸気室(2b)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,第一蒸気室(2a)には,それぞ
れの開閉弁を有する水蒸気管路(13),冷却水管路
(11),真空管路(12)及びドレン管路(17)が
連通している。また,第一蒸気室(2a)は,隙間(2
0)を介してキャビティ(3)に連通する小室(21)
と蒸気孔(2c)にて連通している。第二蒸気室(2
b)には,それぞれの開閉弁を有する水蒸気管路(1
5),冷却水管路(14)及びドレン管路(16)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 second steam chamber (2b) is located on the cavity (3) side, and the first steam chamber (2a) is located outside the second steam chamber (2b). Each steam chamber has a completely independent structure without communication with each other. The first steam chamber (2a) communicates with a steam pipe (13), a cooling water pipe (11), a vacuum pipe (12), and a drain pipe (17) each having an on-off valve. The first steam chamber (2a) is provided with a gap (2
Small chamber (21) communicating with cavity (3) via 0)
And a vapor hole (2c). Second steam chamber (2
b) has a steam line (1
5), the cooling water pipe (14) and the drain pipe (16) communicate with each other.

【0014】本例においては,先ず,水蒸気管路(1
0),(15)の弁及びドレン管路(16),(18)
の弁を開放し,キャビ型(1),コア型(2)のそれぞ
れの第二蒸気室(1b),(2b)に高温の蒸気を導入
して金型を予熱しながら密閉する。次いで,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)に圧縮充填する。この際,充填
ノズル(5)より発泡粒子と共にキャビティ(3)に流
れこむ圧縮空気は隙間(20)より小室(21)及び
(22)と蒸気孔(1c)及び(2c)を経て,両金型
の第一蒸気室(1a)及び(2a)を通過し,開放状態
にあるドレン弁(19)及び(17)より排出する。な
お,発泡粒子の圧縮量は圧縮率から求める。
In this embodiment, first, the steam line (1)
0), (15) valve and drain line (16), (18)
Is opened, high-temperature steam is introduced into the second steam chambers (1b) and (2b) of the mold mold (1) and the core mold (2), respectively, and the mold is sealed while preheating. Next, the expanded particles stored in the compression filling tank (4) are filled with a filling nozzle (5).
To compress and fill the cavity (3). At this time, the compressed air flowing into the cavity (3) together with the foamed particles from the filling nozzle (5) passes through the small chambers (21) and (22) and the steam holes (1c) and (2c) from the gap (20). After passing through the first steam chambers (1a) and (2a) of the mold, they are discharged from the drain valves (19) and (17) in the open state. The amount of compression of the expanded particles is determined from the compression ratio.

【0015】次いで,両金型の第二蒸気室(1b)及び
(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(16),(18)の弁を閉じ,更に両金型の
第二蒸気室(1b)及び(2b)の金型をキャビティ
(3)内の発泡粒子の融点以上まで加熱する。
Next, when the mold temperatures of the second steam chambers (1b) and (2b) of both molds reach a certain temperature or higher, the valves of the drain pipes (16) and (18) are closed, and both molds are further closed. The molds of the second steam chambers (1b) and (2b) of the mold are heated to a temperature equal to or higher than the melting point of the foamed particles in the cavity (3).

【0016】そして,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形成に伴って一定の値から
低下して特定値に到達したとき,両金型の真空管路
(7)及び(12)弁を開放し,ドレン管路(17),
(19)弁を閉じ,蒸気室(1a),(2a)及びキャ
ビティ(3)内を真空排気した後,真空管路(7)及び
(12)弁を閉じ,キャビティ(3)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(8)及び/又は
(13)より導入して加熱する。水蒸気は,水蒸気管路
(8)及び/又は(13)より第一蒸気室(1a)及び
/又は(2a)を通り,蒸気孔(1c)及び/又は(2
c)を介して小室(21)及び/又は(22)を通過
し,隙間(20)よりキャビティ(3)に流入し,発泡
粒子を加熱する。
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 a specific value, the vacuum channels (7) and (12) Open the valve, drain line (17),
(19) After closing the valve and evacuating the steam chambers (1a) and (2a) and the cavity (3), the vacuum lines (7) and (12) are closed and the expanded particles in the cavity (3) are closed. Steam having a temperature necessary for fusion is introduced from the steam line (8) and / or (13) and heated. The steam passes through the first steam chamber (1a) and / or (2a) from the steam line (8) and / or (13), and passes through the steam holes (1c) and / or (2).
After passing through the small chambers (21) and / or (22) via c), it flows into the cavity (3) through the gap (20) and heats the foamed particles.

【0017】次いで,水蒸気管路(8),(10),
(13)及び(15)の弁を閉じ,ドレン管路(1
6),(17),(18)及び(19)の弁を開放し,
冷却水管路(9)及び(14)の弁も開放する。両金型
の第二蒸気室(1b)及び(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, the steam lines (8), (10),
Close the valves of (13) and (15) and set the drain line (1
6) Open the valves of (17), (18) and (19),
The valves in the cooling water lines (9) and (14) are also opened. After cooling the dies by introducing cooling water into the second steam chambers (1b) and (2b) of both dies, the compacts are taken out.

【0018】図2に示す金型は,本例に使用する発泡成
形用金型の別例の概略を示す断面図である。図2に示す
金型はキャビ型(1)の内部に蒸気室(1b)のみを有
している。更に蒸気室(1b)を貫通し,キャビティ
(3)内に水蒸気を導入するためのノズル(23)を有
している。
The mold shown in FIG. 2 is a cross-sectional view schematically showing another example of the foam molding mold used in the present embodiment. The mold shown in FIG. 2 has only the steam chamber (1b) inside the mold (1). Further, it has a nozzle (23) for penetrating the steam chamber (1b) and for introducing steam into the cavity (3).

【0019】図2の金型を用いる場合,蒸気室(1b)
及び(2b)を加熱した状態で,発泡粒子をキャビティ
(3)に圧縮充填し,更に蒸気室(1b)及び(2b)
をキャビティ(3)内の発泡粒子の融点以上に加熱しな
がら,キャビティ(3)内に充填された発泡粒子の所定
面圧力に到達した後,真空管路(12)より第一蒸気室
(2a)及びキャビティ(3)内を真空排気するまでの
工程は前述した図1の金型を用いる成形に準じて行う。
続いて,キャビティ(3)内の発泡粒子を融着するのに
必要な温度の水蒸気を真空管路(12)を閉じた後に,
水蒸気管路(8)よりノズル(23)を介してキャビテ
ィ(3)内に導入し,発泡粒子を加熱する。
When the mold shown in FIG. 2 is used, the steam chamber (1b)
While heating (2b), the foamed particles are compression-filled into the cavity (3), and the steam chambers (1b) and (2b)
While heating to a predetermined surface pressure of the foamed particles filled in the cavity (3) while heating the gas to a temperature equal to or higher than the melting point of the foamed particles in the cavity (3), the first steam chamber (2a) is passed through the vacuum line (12). The steps until the inside of the cavity (3) is evacuated are performed according to the above-described molding using the mold shown in FIG.
Subsequently, after closing the vacuum line (12) with steam at a temperature necessary for fusing the foamed particles in the cavity (3),
The foamed particles are introduced into the cavity (3) through the steam line (8) via the nozzle (23) and heated.

【0020】次いで,水蒸気管路(8)の弁を閉じ,ド
レン管路(16),(17)及び(18)の弁を開放
し,冷却水管路(9)及び(11)の弁も開放する。蒸
気室(1b)及び第二蒸気室(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, the valve of the steam line (8) is closed, the valves of the drain lines (16), (17) and (18) are opened, and the valves of the cooling water lines (9) and (11) are also opened. I do. After cooling the mold by introducing cooling water into the steam chamber (1b) and the second steam chamber (2b), the compact is taken out.

【0021】次に,本発明において用いる発泡粒子とし
ては,ポリスチレン系発泡粒子,ポリエチレン系発泡粒
子,ポリプロピレン系発泡粒子などが挙げられる。ポリ
スチレン系発泡粒子としては,基材樹脂としてスチレン
単量体が50重量%以上含まれる組成で重合されたり,
混合されたものであり,例えば,スチレン単独重合体,
スチレン−アクリロニトリル共重合体,スチレン−アク
リロニトリル−ブタジエン共重合体やこれらのゴム等で
の変性物である。
The expanded particles used in the present invention include expanded polystyrene particles, expanded polyethylene particles, expanded polypropylene particles, and the like. As polystyrene-based expanded particles, as a base resin, a styrene monomer is polymerized in a composition containing 50% by weight or more,
Mixed, for example, styrene homopolymer,
It is a styrene-acrylonitrile copolymer, a styrene-acrylonitrile-butadiene copolymer or a modified product thereof with a rubber or the like.

【0022】ポリエチレン系発泡粒子としては,基材樹
脂としてエチレン単量体が50重量%以上含まれる組成
で重合されたり,混合されたものであり,例えば,高圧
法低密度ポリエチレン,中・高密度ポリエチレン,直鎖
法低密度ポリエチレン,エチレン−酢酸ビニル共重合
体,エチレン−アクリル酸エステル共重合体やこれらの
変性物である。ポリプロピレン系発泡粒子としては,基
材樹脂としてプロピレン単量体が50重量%以上含まれ
る組成で重合されたり,混合されたものであり,例え
ば,プロピレン単独重合体,エチレン−プロピレン共重
合体,ブテン−プロピレン共重合体やこれらの変性物で
ある。
The polyethylene-based foamed particles are polymerized or mixed with a composition containing 50% by weight or more of an ethylene monomer as a base resin. For example, high-pressure low-density polyethylene, medium-high density Polyethylene, linear low-density polyethylene, ethylene-vinyl acetate copolymer, ethylene-acrylate copolymer and modified products thereof. The polypropylene-based foamed particles are polymerized or mixed with a composition containing 50% by weight or more of a propylene monomer as a base resin. Examples thereof include a propylene homopolymer, an ethylene-propylene copolymer, and butene. -Propylene copolymers and modified products thereof.

【0023】これらの発泡粒子は,圧縮空気により圧縮
充填タンク(4)内で圧縮された後,金型のキャビティ
(3)内に均一に圧縮充填される。金型のキャビティ
(3)内に充填された発泡粒子は,加熱されてスキン層
を形成するため,金型のキャビティ(3)に接触した一
部の発泡粒子が熱収縮し,体積が1/30〜1/50に
減少する。その熱収縮により形成された空間を埋めるた
め,キャビティ(3)内に充填された発泡粒子は膨張す
る。しかし,充填率が低くしかも反発力が小さい場合
は,空間を充分に埋めることが出来ない。その結果,得
られた成形体は,収縮して良好な外観を確保出来ない。
These foamed particles are compressed in a compression filling tank (4) by compressed air, and then uniformly compressed in a cavity (3) of a mold. Since the foamed particles filled in the mold cavity (3) are heated to form a skin layer, a part of the foamed particles in contact with the mold cavity (3) are thermally contracted, and the volume is reduced to 1 /. Decrease by 30 to 1/50. In order to fill the space formed by the heat shrinkage, the foam particles filled in the cavity (3) expand. However, when the filling rate is low and the repulsion is small, the space cannot be sufficiently filled. As a result, the obtained molded body shrinks, and a good appearance cannot be secured.

【0024】本発明における発泡粒子加熱の特徴は,ス
キン層を加熱するための加熱条件として,キャビティ
(3)内に充填された発泡粒子の面圧力(反発力)を制
御する点にある。即ち,キャビティ(3)内に充填され
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。この面圧力を適度な範囲で制御することによ
り,良好なスキン層を備えた成形体が得られる。
The feature of the foamed particle heating in the present invention is that the surface pressure (repulsive force) of the foamed particles filled in the cavity (3) is controlled as a heating condition for heating the skin layer. That is, although the foamed particles filled in the cavity (3) have a surface pressure higher than the atmospheric pressure, the volume of the foamed particles decreases with the formation of the skin layer.
The surface pressure, which was higher than the atmospheric pressure, decreases with the formation of the skin layer. By controlling the surface pressure in an appropriate range, a molded article having a good skin layer can be obtained.

【0025】本発明において,上記の面圧力は,0.0
1〜1.5kg/cm2 Gの範囲とされる。面圧力が
0.01kg/cm2 G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するため,
融着不良,成形体の収縮,スキン層部とスキン層部位外
の剥離現象等が起こり,良好な成形体が得られない。一
方,面圧力が1.5kg/cm2 Gを越える場合,発泡
粒子を融着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。
In the present invention, the above surface pressure is 0.0
The range is 1 to 1.5 kg / cm 2 G. If the surface pressure is less than 0.01 kg / cm 2 G, when the foamed particles are heated and fused with steam, the foamed particles are excessively foamed.
Insufficient fusion, shrinkage of the molded body, and peeling phenomena between the skin layer and the outside of the skin layer occur, and a good molded body cannot be obtained. On the other hand, when the surface pressure exceeds 1.5 kg / cm 2 G, the steam introduced for fusing the foamed particles does not penetrate into the inside of the foamed particles. Good molded products cannot be obtained.

【0026】また,本発明の好ましい態様において,発
泡粒子の充填の際,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
の(I)の数式により求めた発泡粒子の圧縮率C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950〜1000kg/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/
3 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 thickness of the molded body other than the skin layer are determined in order to ensure the strength and quality of the molded body at the time of filling the expanded particles. Is set in advance, and the compression ratio C of the expanded particles obtained by the following equation (I) is used. Incidentally, the density of the solid state of the expanded polystyrene particles is 950 to 1000 kg / m 3 , and the density of the expanded polypropylene particles is 850 to 900 kg / m 3 .
m is 3.

【0027】 C=(1−ρ1 /((ρ2 ×2t2 +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 / ((ρ 2 × 2t 2 + ρ 3 × t 3) / t 1)) × 100 (I) C; compression ratio (%) ρ 1; density of foamed resin particles before filling (kg / m 3 ) ρ2: Density of skin layer portion (kg / m 3 ) ρ3: Density other than skin layer portion (kg / m 3 ) t1; thickness of molded body (mm) t2; thickness of skin layer portion (mm) t3; skin Thickness other than layer (mm)

【0028】本発明において,発泡粒子の圧縮率は3〜
70%とするのが好ましい。圧縮率が3%未満では,発
泡粒子の充填量が不足し,スキン層が出来にくく,成形
体が収縮する。また,圧縮率が70%を越えるとスキン
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,更に,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 from 3 to
It is preferably set to 70%. If the compression ratio is less than 3%, the filling amount of the expanded particles is insufficient, a skin layer is hardly formed, and the molded product shrinks. On the other hand, if the compression ratio exceeds 70%, the skin layer can be made thicker, but the heating and melting time will be longer, and the amount of compressed air used for compression filling will increase, thus increasing the production cost.

【0029】本発明においては,スキン層形成後に内部
粒子の融着がより良好な成形体を得るため,金型内に残
存する発泡粒子間の空気を排出させた後,通常,融点未
満,好ましくは融点未満から融点−20℃以上の温度ま
での水蒸気を発泡粒子間に直接導入し,発泡粒子を加熱
融着させる。水蒸気は,成形金型を加熱する熱媒として
も作用する。即ち,水蒸気加熱によれば,その大きな熱
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。
In the present invention, in order to obtain a molded body having better fusion of the internal particles after the formation of the skin layer, after the air between the foamed particles remaining in the mold is discharged, it is usually lower than the melting point, preferably. In this method, steam having a temperature from a temperature lower than the melting point to a temperature higher than the melting point of −20 ° C. is directly introduced between the foamed particles, and the foamed particles are heated and fused. Water vapor also acts as a heating medium for heating the molding die. That is, according to the steam heating, a large amount of heat can be used to efficiently obtain a uniform temperature in a short time.

【0030】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
発明はその要旨を越えない限り,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,上記した
図1に示す装置を使用し,縦200mm,横400m
m,高さ250mm及び肉厚30mm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 thereof. In the embodiment, the apparatus shown in FIG.
m, a height of 250 mm, and a wall thickness of 30 mm were used as a box-shaped mold. 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.

【0031】<圧縮率>圧縮率は,(1−発泡粒子密度
/成形体密度)×100%で求めた。 <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。 <収縮>収縮は,成形体の寸法が金型に対し5/100
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。 <外観>外観は,成形体のスキン層部が平滑で,スキン
層部以外との剥離が無い場合を「良」,スキン層部が平
滑でない場合か,スキン層部以外との剥離がある場合を
「不良」とした。
<Compression Ratio> The compression ratio was determined by (1−expanded particle density / molded product density) × 100%. <Fusion Degree> The degree of fusion was evaluated by the ratio of the area of the molded body which was fractured and cracked other than at the interface of the foamed particles to the total fracture area. <Shrinkage> Shrinkage is measured when the size of the molded product is 5/100
The case of the above decrease was defined as “present”, and the case of less than 5/100 was defined as “absent”. <Appearance> The appearance is “good” when the skin layer portion of the molded product is smooth and there is no peeling from the portion other than the skin layer portion, and when the skin layer portion is not smooth or when there is peeling from the portion other than the skin layer portion. Is "poor".

【0032】実施例1 表1に示すごとく,スキン層部の厚さが0.3mm,ス
キン層密度が850kg/m3 ,スキン層以外の密度が
50kg/m3 ,成形体の全体の肉厚が30mmの成形
体を製造するため,前記(I)の数式より圧縮率約50
%を算出した。密度33kg/m3 のポリプロピレン発
泡粒子を,図1に示した圧縮充填タンク(4)に充填
し,次いで,水蒸気管路(10),(15)の弁及びド
レン管路(16),(18)の弁を開放し,両金型の第
二蒸気室(1b),(2b)に175℃の水蒸気を導入
して金型を予熱しながら密閉した。
Example 1 As shown in Table 1, the thickness of the skin layer was 0.3 mm, the density of the skin layer was 850 kg / m 3 , the density other than the skin layer was 50 kg / m 3 , and the overall thickness of the molded body. Has a compression ratio of about 50 from the above formula (I) in order to produce a compact having a thickness of 30 mm.
% Was calculated. The foamed polypropylene particles having a density of 33 kg / m 3 are filled into the compression filling tank (4) shown in FIG. 1, and then the valves of the steam lines (10) and (15) and the drain lines (16) and (18) ) Was opened, and steam was introduced at 175 ° C. into the second steam chambers (1b) and (2b) of both molds, and the molds were sealed while preheating.

【0033】キャビティ(3)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。
両金型の第二蒸気室(1b),(2b)の金型温度が1
00℃以上に到達したとき,ドレン管路(16),(1
8)の弁を閉じ,両金型の第二蒸気室(1b),(2
b)を加熱した。両金型の第二蒸気室(1b),(2
b)の金型温度は,170℃まで急速に昇温し安定し
た。
A compression filling tank (4) is provided in the cavity (3).
The foamed particles were compression-filled with a filling nozzle (5).
The mold temperature of the second steam chambers (1b) and (2b) of both molds is 1
When the temperature reaches 00 ° C or more, the drain pipes (16), (1)
8) Close the valve and set the second steam chambers (1b) and (2
b) was heated. The second steam chambers (1b) and (2
The mold temperature of b) rapidly rose to 170 ° C. and was stabilized.

【0034】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/cm2 Gを示し
た。面圧力は,図3に示すように低下した。面圧力が
0.5kg/cm2 Gに到達したとき,真空管路
(7),(12)弁を開放し,ドレン管路((17),
(19)弁を閉じ,両金型の第一蒸気室(1a),(2
a)及びキャビティ(3)内を真空排気した後,真空管
路(7),(12)弁を閉じ,発泡粒子の融点未満の水
蒸気を水蒸気管路(8),(13)より導入して加熱し
た。発泡粒子は,水蒸気管路(8)及び(13)より第
一蒸気室(1a)及び(2a)を通り,蒸気孔(1c)
及び(2c)を経て,小室(21)及び(22)を通過
し,隙間(20)を介してキャビティ(3)に流入した
水蒸気により加熱された。水蒸気温度は150℃であ
り,保持時間は15秒であった。
At this time, the surface pressure of the foamed particles filled in the cavity (3) was 1.6 kg / cm 2 G. The surface pressure decreased as shown in FIG. When the surface pressure reaches 0.5 kg / cm 2 G, the vacuum lines (7) and (12) are opened and the drain line ((17),
(19) The valves are closed and the first steam chambers (1a) and (2
After evacuation of a) and the cavity (3), the valves of the vacuum lines (7) and (12) are closed, and steam having a melting point lower than the melting point of the foamed particles is introduced from the steam lines (8) and (13) and heated. did. The expanded particles pass through the first steam chambers (1a) and (2a) from the steam lines (8) and (13), and pass through the steam holes (1c).
After passing through (2c) and (2c), they were heated by the steam flowing through the small chambers (21) and (22) and flowing into the cavity (3) through the gap (20). The steam temperature was 150 ° C. and the retention time was 15 seconds.

【0035】次いで,水蒸気管路(8),(13)の弁
を閉め,ドレン管路(16),(17),(18)及び
(19)の弁も開放した。両金型の第二蒸気室(1
b),(2b)に冷却水を導入し,金型を40℃まで冷
却した後,成形体を金型から取り出した。取り出した成
形体は,その略全面に均一かつ高密度で硬いスキン層を
有していた。また,そのスキン層の密度,厚み及び成形
体の融着,収縮,外観等は箱状成形体の底部とそれ以外
の側面立ち上がり部に関し実質的に同一の性状であっ
た。結果を表1に示す。
Next, the valves of the steam lines (8) and (13) were closed, and the valves of the drain lines (16), (17), (18) and (19) were also opened. The second steam chamber of both molds (1
After cooling water was introduced into b) and (2b) and the mold was cooled to 40 ° C., the molded body was taken out from the mold. The removed molded article had a uniform, high-density, and hard skin layer over substantially the entire surface. The density and thickness of the skin layer and the fusion, shrinkage, appearance and the like of the molded product were substantially the same in the bottom portion of the box-shaped molded product and the other side rising portions. Table 1 shows the results.

【0036】実施例2 表1に示す条件を採用し,キャビティ(3)内に48k
g/m3 のポリプロピレン発泡粒子を圧縮充填し,面圧
力が0.4kg/cm2 G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った。結果を表
1に示す。
Example 2 The conditions shown in Table 1 were adopted, and 48 k
The molding was performed under the same conditions as in Example 1 except that foamed polypropylene particles of g / m 3 were compression-filled, and when the surface pressure reached 0.4 kg / cm 2 G, evacuation was performed. Table 1 shows the results.

【0037】比較例1 発泡粒子の面圧力が0kg/cm2 G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った。結果
を表1に示す。
Comparative Example 1 Molding was performed under the same conditions as in Example 1 except that when the surface pressure of the foamed particles was 0 kg / cm 2 G, vacuum evacuation was performed. Table 1 shows the results.

【0038】比較例2 発泡粒子の面圧力が1.6kg/cm2 G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った。
結果を表1に示す。
Comparative Example 2 Molding was performed under the same conditions as in Example 1 except that when the surface pressure of the expanded particles was 1.6 kg / cm 2 G, the evacuation was performed.
Table 1 shows the results.

【0039】比較例3 金型を30mm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
立ち上がり部の平均圧縮率が10.7%となる条件を採
用した。その他は,実施例1と同一条件で成形を行っ
た。結果を表1に示す。
COMPARATIVE EXAMPLE 3 The mold was changed to cracking filling with an opening of 30 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 rising portion on the side was 10.7%. The conditions were adopted. Otherwise, molding was performed under the same conditions as in Example 1. Table 1 shows the results.

【0040】[0040]

【表1】 [Table 1]

【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,成形体の略全面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 product having a uniform, high-density and hard skin layer on almost the entire surface of the molded product 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を
示す断面説明図。
FIG. 1 is an explanatory sectional view showing an example of a mold for producing a molded article according to the present invention.

【図2】本発明における成形体を製造する金型の他の一
例を示す断面説明図。
FIG. 2 is an explanatory sectional view showing another example of a mold for producing a molded article according to the present invention.

【符号の説明】[Explanation of symbols]

1...キャビ型, 2...コア型, 1a,2a...第一蒸気室, 1b,2b...第二蒸気室, 1c,2c...蒸気孔, 3...キャビティ, 4...圧縮充填タンク, 5...充填ノズル, 6, 9, 11, 14 ...冷却水管路, 7,12...真空管路, 8,10,13,15...水蒸気管路, 16, 17, 18, 19...ドレン管路, 20...隙間, 21,22...小室, 23...水蒸気ノズル, 1. . . Mold type, 2. . . Core type, 1a, 2a. . . First steam chamber, 1b, 2b. . . Second steam chamber, 1c, 2c. . . Steam holes, 3. . . Cavity, 4. . . Compression filling tank, 5. . . Filling nozzles, 6, 9, 11, 14,. . . Cooling water line, 7,12. . . Vacuum line, 8, 10, 13, 15. . . Steam line, 16, 17, 18, 19; . . Drain line, 20. . . Gap, 21, 22,. . . Komuro, 23. . . Steam nozzle,

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及びコア
型からなる発泡成形用金型内に発泡樹脂粒子を充填し加
熱融着させる成形体の製造方法に於いて,金型内に発泡
樹脂粒子を圧縮充填し,上記の両方の蒸気室ともに水蒸
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
て成形体表面にスキン層を形成し,金型に充填した発泡
樹脂粒子の面圧力が0.01〜1.5kg/cm2 Gの
範囲にあるとき,金型内に残存する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。
1. A method for producing a molded article in which foamed resin particles are filled and heated and fused in a foaming mold having a mold cavity and a core mold each having a steam chamber. The particles are compressed and filled, steam is introduced into both of the above-mentioned steam chambers to heat the mold to a temperature higher than the melting point of the foamed resin particles, and the foamed resin particles in contact with the mold are melted to form a surface of the molded body. When a skin layer is formed and the surface pressure of the foamed resin particles filled in the mold is in the range of 0.01 to 1.5 kg / cm 2 G, air between the foamed resin particles remaining in the mold is discharged. A method for producing a molded article having a high-density skin layer, characterized in that steam having a melting point lower than that of the foamed resin is introduced between the foamed resin particles and the foamed resins are heated and fused to each other.
【請求項2】 請求項1に記載の成形体の製造方法にお
いて,下記(I)式の数字で示される圧縮率Cが3〜7
0%の範囲になる様に発泡粒子の充填を行うことを特徴
とする高密度のスキン層を持つ成形体の製造方法。 C=(1−ρ1 /((ρ2 ×2t2 +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 method of manufacturing a molded article according to claim 1, wherein the compression ratio C represented by the following formula (I) is 3-7.
A method for producing a molded article having a high-density skin layer, characterized in that foaming particles are filled so as to be in a range of 0%. C = (1−ρ1 / ((ρ2 × 2t2 + ρ3 × t3) / t1)) × 100 (I) C: Compressibility (%) ρ1; Density of foamed resin particles before filling (kg / m 3 ) ρ2; Density of layer part (kg / m 3 ) ρ3; Density other than skin layer part (kg / m 3 ) t1; Thickness of molded body (mm) t2; Thickness of skin layer part (mm) t3; Thickness (mm)
【請求項3】 請求項1又は2に記載の成形体の製造方
法において,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及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。
3. The method for producing a molded article according to claim 1, wherein the expanded resin particles are polystyrene resin particles,
A method for producing a molded article having a high-density skin layer, wherein the molded article is at least one selected from the group consisting of polyethylene resin particles and polypropylene resin particles.
JP32222097A 1997-11-06 1997-11-06 Method for producing molded body having high density skin layer Expired - Fee Related JP3859330B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32222097A JP3859330B2 (en) 1997-11-06 1997-11-06 Method for producing molded body having high density skin layer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32222097A JP3859330B2 (en) 1997-11-06 1997-11-06 Method for producing molded body having high density skin layer

Publications (2)

Publication Number Publication Date
JPH11138575A true JPH11138575A (en) 1999-05-25
JP3859330B2 JP3859330B2 (en) 2006-12-20

Family

ID=18141293

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32222097A Expired - Fee Related JP3859330B2 (en) 1997-11-06 1997-11-06 Method for producing molded body having high density skin layer

Country Status (1)

Country Link
JP (1) JP3859330B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110086216A1 (en) * 2009-10-13 2011-04-14 Samsung Electronics Co., Ltd. Foamed resin product and foamed resin molding machine to manufacture the same
KR101328746B1 (en) * 2011-06-13 2013-11-11 (주)우남케미칼 method for molding cladding of expanded polystyrene foam
JP2018534175A (en) * 2015-10-13 2018-11-22 クラルマン クンストシュトッフフェアアルバイトゥング ゲーエムベーハー Apparatus and method for producing molded article comprising expanded particles
JP2021030440A (en) * 2019-08-13 2021-03-01 Daisen株式会社 Manufacturing method of foamed resin molded products

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110086216A1 (en) * 2009-10-13 2011-04-14 Samsung Electronics Co., Ltd. Foamed resin product and foamed resin molding machine to manufacture the same
KR101328746B1 (en) * 2011-06-13 2013-11-11 (주)우남케미칼 method for molding cladding of expanded polystyrene foam
JP2018534175A (en) * 2015-10-13 2018-11-22 クラルマン クンストシュトッフフェアアルバイトゥング ゲーエムベーハー Apparatus and method for producing molded article comprising expanded particles
JP2021030440A (en) * 2019-08-13 2021-03-01 Daisen株式会社 Manufacturing method of foamed resin molded products

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