JPH09136331A - Method for in-mold molding of thermoplastic resin foam molding - Google Patents

Method for in-mold molding of thermoplastic resin foam molding

Info

Publication number
JPH09136331A
JPH09136331A JP7295185A JP29518595A JPH09136331A JP H09136331 A JPH09136331 A JP H09136331A JP 7295185 A JP7295185 A JP 7295185A JP 29518595 A JP29518595 A JP 29518595A JP H09136331 A JPH09136331 A JP H09136331A
Authority
JP
Japan
Prior art keywords
filling
mold
molding
particles
pressure
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
JP7295185A
Other languages
Japanese (ja)
Other versions
JP3565636B2 (en
Inventor
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 JP29518595A priority Critical patent/JP3565636B2/en
Publication of JPH09136331A publication Critical patent/JPH09136331A/en
Application granted granted Critical
Publication of JP3565636B2 publication Critical patent/JP3565636B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a foam molding with good appearance and sufficiently performed welding by only one filling when a molded item with different densities is manufactured by means of one molding machine by filling foaming particles each with a different inner pressure are simultaneously filled in a mold through independent filling holes. SOLUTION: When molding is performed by filling foaming particles by compression filling, even if the filling condition is the same, the foaming particles with a low inner pressure generate remarkable shrinkage by the outer pressure during filling (in a method for compression filling, as the pressures in a raw material feeding tank 7' and a mold 4 is elevated at least to an atmospheric pressure, the outer pressure acts on the foaming particles). Therefore, the compression ratio becomes high by filling to obtain a molded article with a high density. On the other hand, as the foaming particles with a high inner pressure has a small pressure difference to the outer pressure during filling, filling is performed by a low compression ratio to obtain a molded article with a low density.

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、異密度の熱可塑性
樹脂発泡成形体の型内成形方法に関するものであり、よ
り詳細には例えば嵩密度が同じ発泡粒子を用いても、成
形工程の工数を増加させることなく、外観の良好な、融
着も十分に行われた、密度の異なる発泡成形体を得る成
形方法に関し、本発明により得られる種々の成形体は、
緩衝材、断熱材、構造部材、芯材等として利用され、特
に自動車部品に有効である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for in-mold molding of thermoplastic resin foam moldings having different densities. More specifically, for example, even when foamed particles having the same bulk density are used, the number of molding steps is increased. Without increasing the appearance, good appearance, fusion was also sufficiently performed, relates to a molding method to obtain a foamed molded product having a different density, various molded products obtained by the present invention,
It is used as a cushioning material, heat insulating material, structural member, core material, etc., and is particularly effective for automobile parts.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】ポリス
チレン、ポリエチレン、ポリプロピレン等の熱可塑性樹
脂の発泡粒子を、型内に充填し、加熱により発泡粒子同
志を融着させて発泡成形体を成形することは従来より工
業的に実施されている。このようにして得られた発泡成
形体はその優れた物性により、緩衝材、断熱材等に広く
利用されている。このようにして得られる発泡成形体の
各種物性は、発泡倍率に大きく依存しているので、緩衝
材として利用される場合、緩衝を必要とする部位の許容
加速度、設計衝突速度、形状等を考慮して発泡成形体の
倍率と寸法が設計される。
2. Description of the Related Art Expanded particles of thermoplastic resin such as polystyrene, polyethylene, polypropylene, etc. are filled in a mold, and the expanded particles are fused by heating to form an expanded molded article. This has been done industrially in the past. The foamed molded product thus obtained is widely used as a cushioning material, a heat insulating material and the like due to its excellent physical properties. Since various physical properties of the foamed molded product obtained in this way largely depend on the expansion ratio, when used as a cushioning material, consider the allowable acceleration of the portion requiring cushioning, the design collision speed, the shape, etc. Then, the magnification and dimensions of the foamed molded product are designed.

【0003】例えばバンパー芯材として衝撃エネルギー
吸収材として使用される場合、フロントバンパー用とリ
アバンパー用にわかれる訳であるが、前記のように設計
を行った結果として異なる発泡倍率が必要となる事が起
こる。このような場合、従来は成形機に、フロント用の
バンパー金型を1つあるいは複数個付けて、必要な所定
量の成形をした後、金型をリアー用のハンパー金型に付
け換えて、再度リア用バンパー芯材の発泡成形体を成形
する方法が実施されてきた。
For example, when it is used as an impact energy absorbing material as a bumper core material, it is divided into a front bumper and a rear bumper. However, as a result of the above design, different expansion ratios may be required. Occur. In such a case, conventionally, one or more front bumper molds were attached to a molding machine, and after molding a required predetermined amount, the mold was replaced with a rear humper mold, The method of molding the foamed molded body of the rear bumper core material has been carried out again.

【0004】一方、同一成形品であっても必要とする物
性上、部位毎に異なる倍率であることが求められる場合
もある。例えば、バンパー芯材として発泡成形体が使用
される場合、正面からの衝撃に対し、発泡体が所定巾歪
むことによって外部からのエネルギーが吸収されるよう
に設計するが、両端のようにライト等の部品がある部位
においては、歪んだ時に割れたり、キズが付いたりする
事があるため、歪量を低く抑えるよう中心部とは異なる
密度であることが望まれる場合がある。
On the other hand, even if the same molded product is used, it is sometimes required that the magnification be different for each part in view of the required physical properties. For example, when a foamed molded product is used as a bumper core material, the foamed product is designed to absorb energy from the outside when the foamed product is distorted by a predetermined width when a shock is applied from the front. Since there is a case where the part having the part of (2) has cracks or scratches when it is distorted, it is sometimes desired that the density be different from that of the central part so as to keep the amount of distortion low.

【0005】これらの製造方法として、それぞれを必要
な倍率で予じめ発泡成形体を成形しておき、次いで発泡
成形体を接着等により一体化する方法が挙げられるが、
この方法ではそれぞれの部分を一体化する手間がかかる
上、その部分に対応した数多くの金型が必要となり、金
型製作費が高額となり、更には工程管理も複雑になると
いう問題があった。
As a method for producing these, there is a method in which each of them is preliminarily molded at a required magnification to form a foamed molded article, and then the foamed molded article is integrated by adhesion or the like.
In this method, there is a problem that it takes time and effort to integrate the respective parts, and many molds corresponding to the parts are required, resulting in high mold manufacturing cost and complicated process control.

【0006】また、もともと密度の異なる発泡粒子を二
種以上用いて、1つの金型内に充填・発泡成形を行う方
法では、低い嵩密度の発泡粒子の充填条件で同時に高い
嵩密度の発泡粒子を充填すると高い嵩密度の発泡粒子が
低い圧縮率で充填されることとなり、成形品としては粒
子間間隙の多い外観不良の成形品しかできない。また逆
に高い嵩密度の発泡粒子の充填条件では、低い嵩密度の
発泡粒子が金型内へ過剰な充填となるため、金型の内部
まで充分に蒸気が通らなくなり成形品の融着が不良なも
のとなるため、従って充填工程でそれぞれの発泡粒子に
合わせた条件を設定する必要が生じるので、複数回の充
填工程を設けなければならないという不都合があった。
Further, in the method of filling and foam-molding in one mold by using two or more kinds of expanded particles having originally different densities, the expanded particles of high bulk density are simultaneously obtained under the filling conditions of expanded particles of low bulk density. In this case, the expanded particles having a high bulk density are filled at a low compression rate, so that only molded products having a poor appearance with many interparticle voids can be obtained. On the contrary, under the filling conditions of expanded particles of high bulk density, expanded particles of low bulk density are excessively filled into the mold, so that steam does not sufficiently reach the inside of the mold and fusion of the molded product is poor. Therefore, it is necessary to set conditions suitable for each foamed particle in the filling step, and there is a disadvantage in that the filling step must be performed a plurality of times.

【0007】[0007]

【課題を解決するための手段】本発明者らは、かかる課
題を解決する為に鋭意研究を重ねた結果、異なる密度の
成形品を1つの成形機で製造するに際して、内圧がそれ
ぞれ異なる粒子を用いることにより、一回の充填で、外
観の良好な融着も十分行われた発泡成形体が得られるこ
とを見い出し、本発明を完成するに至った。即ち、本発
明は熱可塑性樹脂発泡粒子を型内に充填し、加熱により
発泡粒子同志を融着させて発泡成形体を成形する方法に
おいて、該発泡粒子が内圧がそれぞれ異なる二種類以上
の複数の発泡粒子からなり、かつ、それぞれを別々の充
填口より同時に型内へ充填することを特徴とする熱可塑
性樹脂発泡成形体の型内成形方法である。尚、二種類以
上の複数の発泡粒子の基材樹脂の示差走査熱量計にて1
0℃/分の速度で昇温した際に得られる融解ピーク温度
の差が15℃以内であるのが好ましい。
Means for Solving the Problems As a result of intensive studies to solve the above problems, the present inventors have found that when molding products having different densities with a single molding machine, particles having different internal pressures are used. It was found that, by using the foamed product once, it is possible to obtain a foamed molded product having a good appearance and sufficient fusion bonding, thereby completing the present invention. That is, the present invention is a method of filling a thermoplastic resin foamed particle in a mold and molding the foamed particle by heating to fuse the foamed particles to each other to form a foamed molded article, in which the foamed particles have a plurality of two or more different internal pressures. An in-mold molding method for a thermoplastic resin foam-molded article, which is composed of foamed particles and is filled into the mold at the same time through separate filling ports. In addition, the differential scanning calorimeter of the base resin of a plurality of foamed particles of two or more
The difference in melting peak temperature obtained when the temperature is raised at a rate of 0 ° C./minute is preferably within 15 ° C.

【発明の実施の形態】BEST MODE FOR CARRYING OUT THE INVENTION

【0008】本発明においては、内圧がそれぞれ異なる
二種類以上の発泡粒子を用いることが必要であり、それ
によって例えば同じ嵩密度の発泡粒子であっても密度の
異なる成形体を得ることができるのである。即ち、内圧
の低い発泡粒子は高い圧縮率で充填され、内圧の高い発
泡粒子は低い圧縮率で充填されることによって、同一の
嵩密度の発泡粒子から、異なる密度の、寸法、外観等良
好な成形品を得ることができる。例えば、圧縮充填によ
って発泡粒子を充填して成形する場合、同一の充填条件
であっても、内圧の低い発泡粒子は充填時の外圧(圧縮
充填法においては、原料供給タンクおよび金型内を大気
圧以上に昇圧するため、発泡粒子に対しては外圧が働
く)によってかなりの収縮が発生するため、充填により
圧縮率は高くなり、従って密度の大きい成形品になる。
一方、内圧の高い発泡粒子は、充填時の外圧に対して、
差圧が小さいため低い圧縮率で充填されることとなり、
従って密度の小さい成形品になる。
In the present invention, it is necessary to use two or more kinds of expanded particles having different internal pressures, whereby molded articles having different densities can be obtained even with expanded particles having the same bulk density. is there. That is, expanded particles having a low internal pressure are packed at a high compression rate, and expanded particles having a high internal pressure are packed at a low compression rate, so that expanded particles having the same bulk density can have different densities, sizes, and appearances. A molded product can be obtained. For example, in the case of filling foamed particles by compression filling and molding, even under the same filling conditions, the foamed particles with a low internal pressure will have a large external pressure at the time of filling (in the compression filling method, the inside of the raw material supply tank and the mold will be large. Since the pressure is increased to atmospheric pressure or more, an external pressure acts on the expanded particles), and a considerable shrinkage occurs. Therefore, the compression rate becomes high due to the filling, and thus a molded product having a high density is obtained.
On the other hand, the expanded particles with high internal pressure are
Since the differential pressure is small, it will be filled at a low compression rate,
Therefore, the molded product has a low density.

【0009】例えば内圧が大気圧の発泡粒子と内圧が
0.5kg/cm2 G以上に高められた発泡粒子を用い
た例により、より具体的に説明する。前者の粒子では嵩
密度が0.1〜0.01g/cm3 であると充填チャン
バー圧力0.5〜5kg/cm2 Gで圧縮率が10〜6
0%程度で充填されることになる。
[0009] For example, more detailed description will be made with reference to an example using expanded particles having an internal pressure of atmospheric pressure and expanded particles having an internal pressure increased to 0.5 kg / cm 2 G or more. In the former particles, if the bulk density is 0.1 to 0.01 g / cm 3 , the compressibility is 10 to 6 at a filling chamber pressure of 0.5 to 5 kg / cm 2 G.
It will be filled at about 0%.

【0010】一方後者の発泡粒子では、内圧が発泡粒子
の外圧であるチャンバー圧力に抗する力となるため、同
じ条件でも圧縮率が0〜40%と低くなる。従って、高
圧縮率によって充填された前者の粒子では、発泡粒子間
の間隙を埋める力として、圧縮に対する復元力が働くと
同時に、発泡粒子自身の有している二次発泡力も寄与し
て、金型通りの密度の高目の成形品が得られる。一方低
圧縮率によって充填された後者の粒子では、発泡粒子間
の間隙を埋める力として発泡粒子内部の圧力による膨張
力と発泡粒子自身の有している二次発泡力が寄与して、
金型通りの密度の低目の成形品が得られることとなる。
このように、いずれの金型でも成形における発泡粒子間
の間隙を埋める機構の差こそあれ、型通りに賦型された
寸法および発泡粒子間の間隙の埋った、外観が優れ、融
着が良好な成形品が、一回の充填工程のみでできる。
On the other hand, in the latter expanded particles, the internal pressure acts as a force against the chamber pressure, which is the external pressure of the expanded particles, so that the compression rate is as low as 0 to 40% under the same conditions. Therefore, in the former particles filled with a high compressibility, a restoring force against compression works as a force to fill the gaps between the expanded particles, and at the same time, the secondary expansion force of the expanded particles themselves contributes to It is possible to obtain a high-density molded product having a mold-like density. On the other hand, in the latter particles filled with a low compressibility, the expansion force due to the pressure inside the expanded particles and the secondary expansion force of the expanded particles themselves contribute as a force to fill the gap between the expanded particles,
It is possible to obtain a molded product having a low density as a mold.
As described above, in any of the molds, there is a difference in the mechanism for filling the gap between the foamed particles in the molding, the dimension imprinted according to the mold and the gap between the foamed particles are filled, the appearance is excellent, and the fusion is good. A simple molded product can be made with only one filling step.

【0011】本発明においては、発泡粒子の内圧は公知
の方法で付与することが出来る。成形品として要求され
る密度と圧縮率を定めておけば必要な発泡粒子の嵩密度
と内圧が決まるので、最適な内圧付与の手段を実施すれ
ば良い。内圧付与手段としては例えば、特公昭51−2
2951号、特開昭61−40334号、特開平1−2
75104号、特開昭58−101025号、特開昭6
0−24933号等の各公報に記載されるように、発泡
粒子を耐圧容器に入れ、窒素、空気、二酸化炭素等の無
機ガスあるいは、プロパン、ブタン、ジクロロジフロロ
メタン等の低沸点の炭化水素やハロゲン化炭化水素を1
種類あるいは2種類以上用いて、加圧下で粒子内部へ含
浸させる事によって実施することができる。
In the present invention, the internal pressure of the expanded particles can be applied by a known method. If the density and compression rate required for the molded product are determined, the required bulk density and the internal pressure of the foamed particles are determined, so that an optimum internal pressure applying means may be implemented. The internal pressure applying means is, for example, Japanese Patent Publication No.
2951, JP 61-40334 A, JP 1-2
75104, JP 58-101025 A, JP 6
As described in each publication such as 0-24933, foamed particles are placed in a pressure resistant container, and an inorganic gas such as nitrogen, air, carbon dioxide, or a low boiling point hydrocarbon such as propane, butane, dichlorodifluoromethane, etc. And halogenated hydrocarbons 1
It can be carried out by impregnating the inside of the particles under pressure with two or more kinds.

【0012】本発明における発泡粒子を構成する熱可塑
性樹脂としては、ポリスチレン系樹脂、ポリエチレン系
樹脂、ポリプロピレン系樹脂等が用いられるが、中でも
ポリエチレン系あるいはポリプロピレン系等のポリオレ
フィン系の樹脂発泡粒子が好ましい。
As the thermoplastic resin constituting the expanded particles in the present invention, polystyrene resin, polyethylene resin, polypropylene resin and the like are used, and among them, polyolefin resin expanded particles such as polyethylene or polypropylene resin are preferable. .

【0013】本発明において、充填に引き続いて蒸気等
の加熱媒体を金型に導入して発泡粒子相互を融着させ、
発泡成形体を得ることになるため、二種類以上の複数の
発泡粒子の原料となる樹脂の融解ピーク温度は近い方
が、融着が充分に行われるので望ましい。特に望ましく
は融解ピーク温度差が15℃以内のもので、更に望まし
くは10℃以内のものである。
In the present invention, after the filling, a heating medium such as steam is introduced into the mold to fuse the foamed particles together,
Since a foamed molded product is obtained, it is desirable that the melting peak temperatures of the resins, which are the raw materials of the plurality of foamed particles of two or more types, are close to each other, because the fusion is sufficiently performed. Particularly preferably, the difference in melting peak temperature is within 15 ° C, and more preferably within 10 ° C.

【0014】この温度差が大きいと、融解ピーク温度の
低い樹脂の発泡粒子に適した加熱温度で加熱した場合に
は、融解ピーク温度の高い樹脂の発泡粒子では加熱不足
により融着が悪くなる。一方、融解ピーク温度の高い樹
脂の発泡粒子に適した加熱温度で加熱した場合には、融
解ピーク温度の低い樹脂の発泡粒子では過剰加熱とな
り、成形品が溶けた状態となり、寸法も著しく収縮した
り、変形等の発生となり好ましくない。以上のことよ
り、本発明において最も好ましくは、原料樹脂の融解ピ
ークが同じである発泡粒子を用いる。尚、本発明におい
て原料樹脂の融解ピーク温度はJIS K7121の方
法に従って示差走査熱量計にて、試量約5mgを毎分1
0℃で加熱した時に記録される曲線において、試量樹脂
の結晶融解時に発生する吸熱ピークの温度を示す。
If the temperature difference is large, when the resin is heated at a heating temperature suitable for the expanded particles of the resin having a low melting peak temperature, the expanded particles of the resin having a high melting peak temperature are insufficiently heated to cause poor fusion. On the other hand, when heated at a heating temperature suitable for foamed particles of resin having a high melting peak temperature, foamed particles of resin having a low melting peak temperature become overheated, the molded product is in a melted state, and the size significantly shrinks. Or deformation may occur, which is not preferable. From the above, in the present invention, it is most preferable to use the expanded particles having the same melting peak of the raw material resin. In the present invention, the melting peak temperature of the raw material resin is measured by a differential scanning calorimeter in accordance with the method of JIS K7121 to a test amount of about 5 mg per minute.
In the curve recorded when heated at 0 ° C., the temperature of the endothermic peak generated during crystal melting of the sample resin is shown.

【0015】本発明において、発泡粒子を製造する方法
は特に限定されるものではなく、従来公知の方法、即ち
いかなる方法も使用することができる。例えば、分解型
発泡剤を含有する樹脂粒子を、発泡剤の分解温度以上に
加熱して発泡させる方法、揮発性発泡剤を含浸した樹脂
粒子を熱して、スチーム等の外部熱源により加熱し発泡
させる方法、揮発性発泡剤を含浸した樹脂粒子を高温高
圧下の雰囲気より、低圧下へ放出し、発泡させる方法、
押出機にて樹脂に発泡剤を溶融混練したものを、細孔を
有するダイより押し出し発泡させたものをカッティング
して得る方法等いずれでも良い。
In the present invention, the method for producing expanded particles is not particularly limited, and a conventionally known method, that is, any method can be used. For example, a method in which resin particles containing a decomposable foaming agent are heated to a temperature equal to or higher than the decomposition temperature of the foaming agent to foam, or resin particles impregnated with a volatile foaming agent are heated and heated by an external heat source such as steam to foam. Method, a method of discharging resin particles impregnated with a volatile foaming agent from a high-temperature and high-pressure atmosphere under a low pressure to foam.
Any method may be used, such as a method in which a resin obtained by melt-kneading a foaming agent with an extruder is extruded from a die having pores and foamed, and then cut.

【0016】このようにして得られる発泡粒子は圧縮充
填、クラッキング充填等の従来の適宜の充填方法で充填
され、加熱されて、発泡成形体となる。尚、本発明の成
形方法は、図1に示すように1つ成形機を用いその中に
金型が複数存在し、加熱等の成形条件を同じにし密度の
異なる成形体を得たい場合や、図2に示すように1つの
成形体で密度の異なる部分を有する成形体を得たい場合
に適用できる。以下、実施例を挙げ、本発明を更に具体
的に説明するが、本発明は特許請求の範囲を越えない限
り、これらの実施例に限定されるものではない。
The expanded beads thus obtained are filled by a conventional appropriate filling method such as compression filling, cracking filling, etc. and heated to form a foamed molded article. The molding method of the present invention uses one molding machine as shown in FIG. 1 in which a plurality of molds are present and the molding conditions such as heating are the same to obtain moldings having different densities. As shown in FIG. 2, the present invention can be applied to the case where it is desired to obtain a molded product having a portion having different densities in one molded product. Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples as long as the scope of the claims is not exceeded.

【0017】[0017]

【実施例】【Example】

実施例1 本実施例は図1にその概略を示す装置を用いて行った。
原料1として、耐圧容器内で内温50℃、初期圧力1.
0kg/cm2 ・Gにて加圧し、4時間後3.0kg/
cm2 ・Gになるよう0.5kg/cm2 /時で昇圧し
ながら加圧処理することにより、内圧1.8kg/cm
2 ・Gに付与された嵩密度30g/lのエチレンプロピ
レンランダム共重合体(エチレン含量2.6重量%、融
解ピーク温度144℃)の発泡粒子と、原料2として内
圧0kg/cm2 ・Gの嵩密度30g/lのエチレン・
プロピレンランダム共重合体(エチレン含量2.6重量
%、融解ピーク温度144℃)の発泡粒子をそれぞれ
7,7′の原料貯蔵タンクに入れ、いずれも外部よりタ
ンク内部が3.0kg/cm 2 ・Gになるように圧縮空
気にて加圧した。原料貯蔵タンクの圧力を保持しなが
ら、2.5kg/cm2 ・Gになるように加圧された金
型キャビティ3,4にそれぞれの発泡粒子を充填した。
この時3,4の圧力は2.5kg/cm2 ・Gに保持し
ていた。キャビティ内の圧力を大気圧とした後3.5k
g/cm2 ・Gの蒸気を導入して粒子同志を融着させ
た。続いて水冷および空冷を行い、成形品の面圧が0.
5kg/cm2 ・Gになったところで金型を開き、3,
4の成形品を取り出した。3の成形品は、密度37.5
g/l(圧縮率20%)で粒子間の間隙もない良好な外
観であった。また4の成形間隙も、密度60g/l(圧
縮率50%)で粒子間の間隙もない良好な外観であり、
成形の工程を増やすことなく、1つの成形機から異密度
の成形品が得られた。
 Example 1 This example was carried out using the apparatus whose outline is shown in FIG.
As a raw material 1, an internal temperature of 50 ° C. and an initial pressure of 1.
0kg / cmTwo・ Pressurize with G and after 4 hours 3.0 kg /
cmTwo・ 0.5kg / cm to become GTwoBoosted at
While applying pressure, the internal pressure is 1.8 kg / cm
Two・ Ethylene propionate with a bulk density of 30g / l given to G
Ren random copolymer (ethylene content 2.6% by weight, melt
With expanded particles having a solution peak temperature of 144 ° C) and as raw material 2
Pressure 0kg / cmTwo-G ethylene with a bulk density of 30 g / l-
Propylene random copolymer (ethylene content 2.6 wt
%, Melting peak temperature 144 ° C.)
Put it in the raw material storage tank 7, 7 '
3.0 kg / cm inside the tank Two・ Compressed to G
I applied pressure. While maintaining the pressure of the raw material storage tank
2.5 kg / cmTwo・ Gold pressed to G
The mold cavities 3 and 4 were filled with the respective foamed particles.
At this time, the pressure of 3 and 4 is 2.5 kg / cmTwo・ Hold to G
I was 3.5k after setting the pressure in the cavity to atmospheric pressure
g / cmTwo・ Introduce G vapor to fuse particles together
Was. Subsequently, water cooling and air cooling are performed, and the surface pressure of the molded product becomes 0.
5 kg / cmTwo・ Open the mold when it reaches G,
The molded product of No. 4 was taken out. The molded product of 3 has a density of 37.5.
g / l (compressibility 20%) with no gap between particles
It was a view. The molding gap of 4 also has a density of 60 g / l (pressure
50%) and good appearance with no gaps between particles,
Different density from one molding machine without increasing the number of molding processes
A molded product of was obtained.

【0018】実施例2 本実施例は図2にその概略を示す装置を用いて行った。
実施例1と同様に内圧1.8kg/cm2 ・Gの嵩密度
30g/lのエチレン・プロピレンランダム共重合体か
らなる、発泡粒子と、内圧0kg/cm2 ・Gの嵩密度
30g/lのエチレン・プロピレンランダム共重合体か
らなる発泡粒子をそれぞれ7,7’の原料貯蔵タンクに
入れ、タンク内部を圧縮空気にて3.0kg/cm2
Gに加圧した。隔壁8によってしきられた金型キャビテ
ィ3′と4′をいずれも2.5kg/cm2 ・Gに加圧
した状態でそれぞれの発泡粒子を充填した。充填終了
後、壁作動シリンダー9にて8のしきりを引き取り、続
いて3.5kg/cm2 ・Gの蒸気にて加熱、更に水
冷、空冷を行い成形した。このようにして得られた成形
品は、3′と4′との境界の部分でも良く融着一体化
し、さらに3′と4′の部分の密度が37.5g/lと
60g/lの異密度であり、どちらの部分も粒子間間隙
もない良好なものであった。
Example 2 This example was carried out using the apparatus whose outline is shown in FIG.
In the same manner as in Example 1, foamed particles composed of an ethylene / propylene random copolymer having an internal pressure of 1.8 kg / cm 2 · G and a bulk density of 30 g / l, and an internal pressure of 0 kg / cm 2 · G having a bulk density of 30 g / l Foamed particles made of ethylene / propylene random copolymer were put in the raw material storage tanks 7, 7 ', respectively, and the inside of the tank was compressed with compressed air to 3.0 kg / cm 2 ·.
Pressurized to G. Each of the mold cavities 3'and 4'which were cut off by the partition wall 8 was filled with respective foamed particles while being pressurized to 2.5 kg / cm 2 · G. After the completion of filling, the wall-operated cylinder 9 was used to remove the threshold value of 8, followed by heating with steam of 3.5 kg / cm 2 · G, followed by water cooling and air cooling for molding. The molded product thus obtained was well fused and integrated even at the boundary between 3'and 4 ', and the densities of 3'and 4'differences of 37.5 g / l and 60 g / l were different. The density was good, and there was no interparticle gap in either part, which was good.

【0019】比較例1 原料貯蔵タンク7,7′に入れる原料がいずれも、内圧
0kg/cm2 ・Gの嵩密度30g/lのエチレン・プ
ロピレンランダム共重合体(エチレン含量2.6重量
%、融解ピーク温度144℃)からなる発泡粒子とする
以外は実施例1と同様に成形を行った。3,4の成形品
はいずれも60g/l(圧縮率50%)で同じ密度であ
った。
Comparative Example 1 The raw materials to be put in the raw material storage tanks 7 and 7'are ethylene / propylene random copolymers (ethylene content 2.6% by weight, internal pressure 0 kg / cm 2 · G, bulk density 30 g / l). Molding was performed in the same manner as in Example 1 except that expanded particles having a melting peak temperature of 144 ° C.) were used. The molded products of Nos. 3 and 4 had the same density at 60 g / l (compression rate 50%).

【0020】比較例2 原料貯蔵タンク7には内圧0kg/cm2 ・Gの嵩密度
15g/lのエチレン・プロピレンランダム共重合体
(エチレン含量2.6重量%、融解ピーク温度144
℃)からなる発泡粒子を入れ、7’には内圧0kg/c
2 ・Gの嵩密度30g/lのエチレン・プロピレンラ
ンダム共重合体(エチレン含量2.6重量%、融解ピー
ク144℃)からなる発泡粒子を入れて成形する以外
は、実施例1と同様に成形を行った。4の成形品は60
g/l(圧縮率50%)で粒子間間隙もなく融着も良好
なものであったが、3の成形品は43g/l(圧縮率6
5%)で粒子間間隙はないものの、全く融着していない
成形品であった。
Comparative Example 2 In the raw material storage tank 7, an ethylene / propylene random copolymer having an internal pressure of 0 kg / cm 2 · G and a bulk density of 15 g / l (ethylene content 2.6% by weight, melting peak temperature 144
℃) foamed particles, and 7'internal pressure 0kg / c
Same as Example 1 except that the foamed particles made of ethylene / propylene random copolymer (ethylene content 2.6% by weight, melting peak 144 ° C.) having a bulk density of m 2 · G of 30 g / l were added and molded. Molded. 4 is 60
At 3 g / l (compressibility of 50%), there was no interparticle gap and good fusion, but the molded product of 3 was 43 g / l (compressibility of 6).
5%), there was no interparticle gap, but the molded article was not fused at all.

【0021】比較例3 原料貯蔵タンク7,7′の圧力を1.5kg/cm2
Gとし、金型キャビティ3,4を1.0kg/cm2
Gとして成形する以外は比較例2と同様に成形を行っ
た。3の成形品は30g/l(圧縮率50%)で粒子間
間隙のない融着良好なものであったが、4の成形品は3
3g/l(圧縮率9%)で粒子間間隙が大きな外観の悪
いものしか得られなかった。
Comparative Example 3 The pressure of the raw material storage tanks 7 and 7'was 1.5 kg / cm 2 ·.
G and the mold cavities 3 and 4 are 1.0 kg / cm 2 ·
Molding was performed in the same manner as Comparative Example 2 except that molding was performed as G. The molded product of 3 was 30 g / l (compression ratio 50%) and had good fusion with no interparticle gap, while the molded product of 4 was 3
At 3 g / l (compressibility 9%), only intergranular gaps and bad appearance were obtained.

【0022】比較例4 原料貯蔵タンク7には内圧1.2kg/cm2 ・Gに付
与された嵩密度47g/lの直鎖状低密度ポリエチレン
(密度0.924g/ml、融解ピーク温度123℃)
からなる発泡粒子を入れ、一方7′には内圧0kg/c
2 ・Gの嵩密度30g/lのエチレン・プロピレン共
重合体(エチレン含量2.6重量%、融解ピーク温度1
44℃)からなる発泡粒子を入れる他は実施例1と同様
に成形を行った。4の成形品は密度60g/l(圧縮率
50%)で粒子間の間隙もなく融着良好なものであった
が、3の成形品は密度80g/l(圧縮率41%)で表
面がケロイド状に融け、全体的に収縮の大きなものであ
った。
Comparative Example 4 In the raw material storage tank 7, linear low-density polyethylene having a bulk density of 47 g / l (density of 0.924 g / ml, melting peak temperature of 123 ° C.) given an internal pressure of 1.2 kg / cm 2 · G. )
Foamed particles consisting of, while 7'internal pressure 0 kg / c
m 2 · G bulk density 30 g / l ethylene / propylene copolymer (ethylene content 2.6% by weight, melting peak temperature 1
Molding was performed in the same manner as in Example 1 except that expanded particles composed of 44 ° C.) were added. The molded product of No. 4 had a density of 60 g / l (compression rate of 50%) and had good fusion without gaps between particles, while the molded product of No. 3 had a density of 80 g / l (compression ratio of 41%) and had a surface It melted like a keloid and had large shrinkage as a whole.

【0023】[0023]

【発明の効果】本発明によると、例えば同一の嵩密度の
発泡粒子を用いても、一回の充填で、外観の良好な、融
着も十分に行われた密度の異なる発泡成形体を得ること
ができる。
EFFECTS OF THE INVENTION According to the present invention, for example, even if expanded particles having the same bulk density are used, a foamed molded article having a good appearance and a sufficient fusion bonding and different densities can be obtained by a single filling. be able to.

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

【図1】本発明の成形方法で使用される金型の一実施例
である。
FIG. 1 is an example of a mold used in the molding method of the present invention.

【図2】本発明の成形方法で使用される金型の他の実施
例である。
FIG. 2 is another example of the mold used in the molding method of the present invention.

【符号の説明】[Explanation of symbols]

1a,2b 金型フレーム 2a,2b インサイドプレート 3a,3b 金型 4a,4b 金型 5,5′ 充填ガン 6,6′ 原料供給ライン 7,7′ 原料貯蔵タンク 8 隔壁 9 壁作動シリンダー 1a, 2b Mold frame 2a, 2b Inside plate 3a, 3b Mold 4a, 4b Mold 5,5 'Filling gun 6,6' Raw material supply line 7,7 'Raw material storage tank 8 Partition wall 9 Wall working cylinder

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 熱可塑性樹脂発泡粒子を型内に充填し、
加熱により発泡粒子同志を融着させて発泡成形体を成形
する方法において、該発泡粒子が内圧がそれぞれ異なる
二種類以上の複数の発泡粒子からなり、かつ、それぞれ
を別々の充填口より同時に型内へ充填することを特徴と
する熱可塑性樹脂発泡成形体の型内成形方法。
1. A thermoplastic resin expanded particle is filled in a mold,
In a method of forming a foamed molded article by fusing foamed particles together by heating, the foamed particles are composed of a plurality of foamed particles of two or more kinds having different internal pressures, and each of them is simultaneously injected into the mold from different filling ports. A method for in-mold molding of a thermoplastic resin foam-molded article, which comprises:
【請求項2】 該二種類以上の複数の発泡粒子の基材樹
脂の示差走査熱量計にて10℃/分の速度で昇温した際
に得られる融解ピーク温度の差が15℃以内であること
を特徴とする、請求項1記載の型内成形方法。
2. A difference in melting peak temperature obtained when the temperature is raised at a rate of 10 ° C./min with a differential scanning calorimeter of the base resin of the plurality of foamed particles of two or more kinds is within 15 ° C. The in-mold molding method according to claim 1, wherein:
JP29518595A 1995-11-14 1995-11-14 In-mold molding method for thermoplastic resin foam Expired - Fee Related JP3565636B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29518595A JP3565636B2 (en) 1995-11-14 1995-11-14 In-mold molding method for thermoplastic resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29518595A JP3565636B2 (en) 1995-11-14 1995-11-14 In-mold molding method for thermoplastic resin foam

Publications (2)

Publication Number Publication Date
JPH09136331A true JPH09136331A (en) 1997-05-27
JP3565636B2 JP3565636B2 (en) 2004-09-15

Family

ID=17817315

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29518595A Expired - Fee Related JP3565636B2 (en) 1995-11-14 1995-11-14 In-mold molding method for thermoplastic resin foam

Country Status (1)

Country Link
JP (1) JP3565636B2 (en)

Also Published As

Publication number Publication date
JP3565636B2 (en) 2004-09-15

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