JPH0647829A - Manufacture of olefin resin internal expansion molding body - Google Patents
Manufacture of olefin resin internal expansion molding bodyInfo
- Publication number
- JPH0647829A JPH0647829A JP5012314A JP1231493A JPH0647829A JP H0647829 A JPH0647829 A JP H0647829A JP 5012314 A JP5012314 A JP 5012314A JP 1231493 A JP1231493 A JP 1231493A JP H0647829 A JPH0647829 A JP H0647829A
- Authority
- JP
- Japan
- Prior art keywords
- mold
- expanded particles
- steam
- temperature
- olefin resin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明はオレフィン系樹脂型内発
泡成形体の製造法に関する。さらに詳しくは、たとえば
各種部材、緩衝材などとして好適に使用しうるオレフィ
ン系樹脂型内発泡成形体の製造法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an olefin resin in-mold foam molded article. More specifically, it relates to a method for producing an olefin-based resin in-mold foam molded article that can be suitably used as, for example, various members and cushioning materials.
【０００２】[0002]
【従来の技術】従来、オレフィン系樹脂型内発泡成形体
は、２枚の蒸気孔を有する金型を型締めした成形型内
に、予備発泡粒子を充填し、該蒸気孔から蒸気を通じる
ことによって加熱、融着する方法によって成形されてい
る。2. Description of the Related Art Conventionally, an olefin-based resin in-mold foam molded article is prepared by filling pre-expanded particles in a mold in which a mold having two steam holes is clamped and passing steam through the steam holes. It is formed by a method of heating and fusing.
【０００３】しかしながら、かかる方法によって成形さ
れた型内発泡成形体は、その両表面に蒸気孔の跡が必ず
残存するため、いずれの表面においても決して外観が美
麗なものとはいえない。However, the in-mold foam molded product molded by such a method cannot be said to have a beautiful appearance on either surface because traces of vapor holes always remain on both surfaces thereof.
【０００４】そこで、一方表面に蒸気孔の跡が残らない
ようにするために、一方の金型にのみ蒸気孔を設け、他
方の金型には蒸気孔を設けないように設計された成形型
を用いて成形する方法が検討されているが、成形型の蒸
気孔を有しない面では、蒸気による加熱が不充分なた
め、予備発泡粒子同士の融着不良が発生し、かえって該
予備発泡粒子形状に基づく凹凸が表面上に発生してしま
うという欠点がある。Therefore, in order to prevent the traces of steam holes from remaining on the surface of one mold, a mold designed to have steam holes only in one mold and not steam holes in the other mold. Although a method of molding using has been studied, in the surface having no steam holes of the molding die, because of insufficient heating by steam, poor fusion of pre-expanded particles occurs, rather the pre-expanded particles There is a drawback that irregularities based on the shape are generated on the surface.
【０００５】したがって、一方の金型の蒸気孔のみから
蒸気を導入することによって蒸気孔を有しない金型面の
予備発泡粒子同士が融着不良を起こさずに成形しうる方
法の確立が、当該技術分野において永年の研究課題とし
て残されていた。Accordingly, the establishment of a method by which the pre-expanded particles on the mold surface having no steam holes can be molded without causing defective fusion by introducing steam from only the steam holes of one mold is concerned. It was left as a long-standing research topic in the technical field.
【０００６】[0006]
【発明が解決しようとする課題】本発明は、前記従来技
術に鑑みて、一方の金型の蒸気孔のみから蒸気を導入す
ることによって蒸気孔を有しない金型面の予備発泡粒子
同士が融着不良を起こさずに成形しうる方法の確立を目
的としてなされたものであり、予備発泡粒子としてオレ
フィン系樹脂予備発泡粒子を用い、なおかつ該オレフィ
ン系樹脂予備発泡粒子を特定の条件下で加熱融着せしめ
て成形したときには、蒸気孔を有しない金型面であって
も融着不良などの発生などがない外観美麗な型内発泡成
形体がえられるというまったく新しい事実を見出し、本
発明を完成するにいたった。DISCLOSURE OF THE INVENTION In view of the above-mentioned prior art, the present invention fuses the pre-expanded particles on the mold surface having no steam holes by introducing steam only from the steam holes of one mold. It was made for the purpose of establishing a method capable of molding without causing poor adhesion, using olefin-based resin pre-expanded particles as pre-expanded particles, and heating the olefin-based resin pre-expanded particles under specific conditions. The present invention has been completed by discovering the completely new fact that when molded by being put on and molded, an in-mold foam molded article with a beautiful appearance can be obtained, even if the mold surface does not have steam holes, such as the occurrence of defective fusion. Came to do.
【０００７】[0007]
【課題を解決するための手段】すなわち、本発明は、蒸
気孔を有しない金型Ａと蒸気孔を有する金型Ｂとを型締
めして成形型を構成したのち、オレフィン系樹脂予備発
泡粒子を該成形型内に充填し、金型Ｂの蒸気孔から水蒸
気を供給し、該予備発泡粒子がたがいに融着する温度よ
りも低い温度で該予備発泡粒子を予備加熱し、該予備発
泡粒子を水蒸気で蒸らし、ついで該予備発泡粒子がたが
いに融着する温度以上の温度で該予備発泡粒子を本加熱
することを特徴とするオレフィン系樹脂型内発泡成形体
の製造法に関する。That is, according to the present invention, a mold A is formed by clamping a mold A having no steam holes and a mold B having steam holes, and then forming olefin resin pre-expanded particles. Is charged into the molding die, steam is supplied from the steam holes of the mold B, and the pre-expanded particles are pre-heated at a temperature lower than the temperature at which the pre-expanded particles are fused to each other. Is steamed with steam, and then the pre-expanded particles are subjected to main heating at a temperature equal to or higher than the temperature at which the pre-expanded particles are fused with each other.
【０００８】[0008]
【作用および実施例】本発明のオレフィン系樹脂型内発
泡成形体の製造法は、予備発泡粒子同士の融着不良をな
くするために、該予備発泡粒子を成形型内で金型の両面
から蒸気などにより加熱しなければならないとされてい
た従来技術の常識を打破するまったく新しい成形型の片
面加熱による型内発泡成形体を提供するものである。OPERATIONS AND EXAMPLES The method for producing an olefin resin in-mold foam molded article of the present invention is to remove the pre-expanded particles from both sides of the mold in order to eliminate defective fusion between the pre-expanded particles. It is an object to provide an in-mold foam molded article by completely heating one side of a completely new molding die that breaks the conventional wisdom that is required to be heated by steam or the like.
【０００９】本発明の型内発泡成形体の製造法によれ
ば、粒子同士の融点不良のない型内発泡成形体を製造す
ることができる理由は、定かではないが、従来のただ単
なる水蒸気による加熱だけでなく、特定の条件下で予備
加熱を行なったのち、蒸らしを行なうという工程が採ら
れているので、金型の水蒸気が導入される側の予備発泡
粒子と金型の水蒸気が導入されない側の予備発泡粒子の
温度差が小さくなり、本加熱による融着性が向上するこ
とによるものと推測することができる。According to the method for producing an in-mold foamed molded product of the present invention, the reason why an in-mold foamed molded product having no defective melting point between particles can be manufactured is not clear, but the conventional simple mere water vapor is used. Not only heating but also preheating under specific conditions and then steaming are performed, so pre-expanded particles on the side where steam of the mold is introduced and steam of the mold are not introduced. It can be presumed that this is because the temperature difference of the pre-expanded particles on the side becomes small and the fusion property by the main heating is improved.
【００１０】以下、本発明のオレフィン系樹脂型内発泡
成形体の製造法の一実施例を図面に基づいて説明する。An embodiment of a method for producing an olefin resin in-mold foamed article of the present invention will be described below with reference to the drawings.
【００１１】図１は、本発明の製造法に用いられる成形
型の一実施態様を示す概略説明図である。FIG. 1 is a schematic explanatory view showing one embodiment of a molding die used in the manufacturing method of the present invention.
【００１２】図１において、蒸気孔を有しない金型Ａ１
は、蒸気孔を有する金型Ｂ２と型締めされている。金型
Ａ１は、たとえばシリンダー３などと連接され、金型Ａ
１を移動させることによって金型Ａ１と金型Ｂ２とを型
締めおよび型開きすることができるように構成されてい
る。金型Ｂ２の内面には、複数の蒸気孔４が設けられて
おり、蒸気導入口５から導入された水蒸気は、金型Ｂ２
の内部６を介して該蒸気孔４を通って成形室７内に導入
される。また、金型Ｂ２内にはフィーダー８が設けられ
ており、かかるフィーダー８により、原料であるオレフ
ィン系樹脂予備発泡粒子が成形室７内に導入される。In FIG. 1, a mold A1 having no steam holes is provided.
Is clamped to a mold B2 having steam holes. The mold A1 is connected to, for example, the cylinder 3 and the like.
By moving the mold 1, the mold A1 and the mold B2 can be clamped and opened. A plurality of steam holes 4 are provided on the inner surface of the mold B2, and the steam introduced from the steam inlet 5 is
Is introduced into the molding chamber 7 through the steam hole 4 through the inside 6 of the. Further, a feeder 8 is provided in the mold B2, and the olefin resin pre-expanded particles as a raw material are introduced into the molding chamber 7 by the feeder 8.
【００１３】本発明の型内発泡成形体の製造法において
は、金型Ａには蒸気孔が設けられておらず、該金型Ａの
内面からは蒸気による予備発泡粒子の加熱は行なわれな
い。In the method for producing an in-mold foam molded article of the present invention, the mold A is not provided with steam holes, and the pre-foamed particles are not heated from the inner surface of the mold A by steam. .
【００１４】なお、えられる型内発泡成形体の表面に所
望の凹凸形状を付与せしめるばあいには、金型Ａの内面
には、たとえば、電蝕、放電加工などの手段によりエン
ボス加工を施しておいてもよい。かかる凹凸形状におい
てはとくに限定がなく、たとえば布目、レザー模様、波
模様などがあげられるが、本発明にはかかる例示によっ
て限定されるものではない。図１においては、金型１の
内面には円柱形状の凹凸が設けられたものの一例が示さ
れている。In the case where the surface of the obtained in-mold foam molded article is given a desired uneven shape, the inner surface of the mold A is embossed by means such as electrolytic corrosion or electric discharge machining. You may keep it. The uneven shape is not particularly limited, and examples thereof include a texture, a leather pattern, and a wave pattern. However, the present invention is not limited thereto. FIG. 1 shows an example in which the inner surface of the die 1 is provided with columnar irregularities.
【００１５】前記金型Ａ１と金型Ｂ２とを型締めしたの
ち、フィーダー８を介してオレフィン系樹脂予備発泡粒
子を成形室７内に充填する。After the mold A1 and the mold B2 are clamped, the olefin resin pre-expanded particles are filled in the molding chamber 7 through the feeder 8.
【００１６】前記オレフィン系樹脂予備発泡粒子に用い
られるオレフィン系樹脂としては、たとえばエチレンホ
モポリマー、プロピレンホモポリマー、エチレン−プロ
ピレンランダムコポリマー、エチレン−プロピレンブロ
ックコポリマー、エチレン−プロピレン−ブテンランダ
ムターポリマー、プロピレン−塩化ビニルコポリマー、
プロピレン−ブテンコポリマー、プロピレン−無水マレ
イン酸コポリマーなどがあげられ、これらは単独でまた
は２種以上を混合して用いてもよい。Examples of the olefin resin used for the pre-expanded olefin resin particles include ethylene homopolymer, propylene homopolymer, ethylene-propylene random copolymer, ethylene-propylene block copolymer, ethylene-propylene-butene random terpolymer and propylene. -Vinyl chloride copolymer,
Examples thereof include a propylene-butene copolymer and a propylene-maleic anhydride copolymer, which may be used alone or in combination of two or more.
【００１７】前記オレフィン系樹脂は、無架橋の状態の
ものが好ましいが、パーオキサイドや放射線などにより
架橋されたものであってもよい。The olefin resin is preferably in a non-crosslinked state, but may be crosslinked with peroxide or radiation.
【００１８】また、前記オレフィン系樹脂として、該オ
レフィン系樹脂と混合しうる他の熱可塑性樹脂が混合さ
れたものを用いてもよい。かかる他の熱可塑性樹脂の具
体例としては、たとえばポリスチレン、ポリブテン、ア
イオノマーなどがあげられ、これらの熱可塑性樹脂の配
合量は、通常前記オレフィン系樹脂100 部（重量部、以
下同様）に対して20部以下、なかんづく５〜10部とする
ことが好ましい。Further, as the olefin resin, a mixture of other thermoplastic resin which can be mixed with the olefin resin may be used. Specific examples of such other thermoplastic resin include, for example, polystyrene, polybutene, ionomer, etc. The blending amount of these thermoplastic resins is usually 100 parts by weight of the olefin resin (weight part, the same applies hereinafter). It is preferably 20 parts or less, especially 5 to 10 parts.
【００１９】前記オレフィン系樹脂は、通常予備発泡さ
れやすいように、あらかじめたとえば押出機、ニーダ
ー、バンバリーミキサー、ロールなどを用いて溶融し、
円柱状、楕円柱状、球状、立方体状、直方体状などの所
望の粒子形状で、その粒子の平均粒径が0.1 〜10mm、好
ましくは0.7 〜５mmとなるように成形加工されることが
望ましい。The olefin resin is usually melted in advance by using, for example, an extruder, a kneader, a Banbury mixer, a roll or the like so that it is easily prefoamed.
It is desirable that the particles have a desired particle shape such as a cylindrical shape, an elliptic cylindrical shape, a spherical shape, a cubic shape, or a rectangular parallelepiped shape, and the average particle diameter of the particles is 0.1 to 10 mm, preferably 0.7 to 5 mm.
【００２０】前記オレフィン系樹脂予備発泡粒子を製造
する方法としては、たとえば耐圧容器中でオレフィン系
樹脂粒子に揮発性発泡剤を含有させ、撹拌しながら水中
に分散させ、加圧下で所定の発泡温度まで加熱したの
ち、該水分散物を低圧域に放出する方法などがあげられ
るが、本発明はかかる方法によって限定されるものでは
ない。As a method for producing the pre-expanded olefin resin particles, for example, a volatile foaming agent is added to the olefin resin particles in a pressure vessel, dispersed in water with stirring, and a predetermined foaming temperature is applied under pressure. Examples of the method include a method in which the water dispersion is discharged to a low pressure region after being heated to the low temperature, but the present invention is not limited to such a method.
【００２１】前記オレフィン系樹脂予備発泡粒子の発泡
倍率は、あまりにも大きすぎるばあいには、えられる型
内発泡成形体の収縮が大きくなったり、柔かくなりすぎ
る傾向があり、またあまりにも小さすぎるばあいには、
緩衝性などが低下する傾向があるので、通常３〜60倍、
好ましくは５〜50倍、さらに好ましくは８〜45倍、とく
に好ましくは10〜35倍であることが望ましい。If the expansion ratio of the olefin resin pre-expanded particles is too large, the obtained in-mold expansion molded article tends to have a large shrinkage or becomes too soft, and too small. In some cases,
Since the buffering property tends to decrease, it is usually 3 to 60 times,
It is preferably 5 to 50 times, more preferably 8 to 45 times, particularly preferably 10 to 35 times.
【００２２】前記オレフィン系樹脂予備発泡粒子をフィ
ーダー８を通じて成形室７内に充填するに際しては、あ
らかじめ予備発泡粒子を加圧ガスを用いて加圧し、該加
圧ガスが該予備発泡粒子中に充分に浸透され、内圧が付
与された状態で成形室７内に充填してもよく、該予備発
泡粒子を加圧ガスを用いて圧縮した状態で成形室７内に
充填してもよく、また該予備発泡粒子に内圧を付与した
り、圧縮することなく、そのままの状態で成形室７内に
充填してもよく、本発明はかかる充填方法によって限定
されるものではない。When the pre-expanded olefin resin particles are filled in the molding chamber 7 through the feeder 8, the pre-expanded particles are preliminarily pressurized with a pressurized gas, and the pressurized gas is sufficiently contained in the pre-expanded particles. Of the pre-expanded particles may be filled in the molding chamber 7 in a state where the pre-expanded particles are compressed with a pressurized gas. The pre-expanded particles may be filled in the molding chamber 7 as they are without applying or compressing the internal pressure, and the present invention is not limited to such a filling method.
【００２３】前記オレフィン系樹脂予備発泡粒子を成形
室７内に充填したのち、金型Ｂ２の蒸気孔４から水蒸気
を供給し、該予備発泡粒子がたがいに融着する温度より
も低い温度で該予備発泡粒子を予備加熱する。After the pre-expanded olefin resin particles have been filled in the molding chamber 7, steam is supplied from the vapor holes 4 of the mold B2 at a temperature lower than the temperature at which the pre-expanded particles fuse with each other. Preheat the pre-expanded particles.
【００２４】本発明においては、前記予備発泡粒子がた
がいに融着する温度よりも低い温度で該予備発泡粒子を
予備加熱する点にも特徴があり、このように該予備発泡
粒子を予備加熱したばあいには、本加熱を行なう前に予
備発泡粒子が融着することなく充分に加熱されている状
態になっており、本加熱により均一にむらなく融着させ
ることができる。なお、本発明において、予備加熱の際
に、予備発泡粒子を融着温度以上の温度に加熱したばあ
には、水蒸気孔側から予備発泡粒子が優先的に融着して
しまい、その結果、金型Ａ側の予備発泡粒子にまで水蒸
気が充分に透過しがたくなり、融着不良が生じるように
なるため、該予備発泡粒子の融着温度よりも低い温度で
予備加熱する。かかる予備発泡粒子の融着温度は、該予
備発泡粒子に用いられている樹脂の種類などによって異
なるので一概には決定することができないため、あらか
じめ該予備発泡粒子の融着温度を調べたのち、金型Ｂ２
の蒸気孔４から導入される水蒸気の温度を設定すること
が好ましい。The present invention is also characterized in that the pre-expanded particles are pre-heated at a temperature lower than the temperature at which the pre-expanded particles are fused together. The pre-expanded particles are pre-heated in this manner. In this case, the pre-expanded particles are in a sufficiently heated state without being fused before the main heating is performed, and the uniform heating can be performed evenly by the main heating. In the present invention, during preheating, when the pre-expanded particles are heated to a temperature equal to or higher than the fusion temperature, the pre-expanded particles are preferentially fused from the water vapor hole side, and as a result, Water vapor does not easily permeate to the pre-expanded particles on the side of the mold A, causing defective fusion, so preheating is performed at a temperature lower than the fusion temperature of the pre-expanded particles. Since the fusion temperature of the pre-expanded particles cannot be unconditionally determined because it varies depending on the type of resin used in the pre-expanded particles, after examining the fusion temperature of the pre-expanded particles in advance, Mold B2
It is preferable to set the temperature of the steam introduced from the steam holes 4 of the above.
【００２５】前記融着温度とは、深さが50mm程度の金型
内に予備発泡粒子を充填し、所定温度（所定圧力）の水
蒸気を10〜20秒間該金型内に導入したときに、予備発泡
粒子同士が融着し、型内発泡成形体の形状を保持するこ
とができる状態となる最低温度をいう。The fusion temperature means the pre-expanded particles filled in a mold having a depth of about 50 mm, and steam at a predetermined temperature (predetermined pressure) is introduced into the mold for 10 to 20 seconds. It is the lowest temperature at which the pre-foamed particles are fused to each other and the shape of the in-mold foam molded article can be maintained.
【００２６】また、予備加熱する際の水蒸気の温度が低
すぎるばあいには、予備加熱による効果が充分に発現さ
れなくなる傾向があるので、水蒸気の温度は、予備発泡
粒子の融着温度以下〜融着温度よりも35℃低い温度以
上、好ましくは融着温度よりも３℃低い温度以下〜融着
温度よりも30℃低い温度以上、より好ましくは融着温度
よりも５℃低い温度以下〜融着温度よりも25℃低い温度
以上とすることが望ましい。If the temperature of the steam during the preheating is too low, the effect of the preheating tends not to be sufficiently exhibited. Therefore, the temperature of the steam is not higher than the fusion temperature of the pre-expanded particles. The temperature is 35 ° C lower than the fusing temperature, preferably 3 ° C lower than the fusing temperature to 30 ° C lower than the fusing temperature, more preferably 5 ° C lower than the fusing temperature to fusing It is desirable that the temperature is 25 ° C lower than the deposition temperature or higher.
【００２７】予備加熱を行なうばあいの水蒸気の圧力
は、水蒸気の温度が前記範囲内となるように適宜調整す
ればよい。The pressure of the steam during the preheating may be appropriately adjusted so that the temperature of the steam is within the above range.
【００２８】つぎに金型Ｂ２の蒸気孔４から水蒸気を供
給して予備加熱をしたのち、水蒸気で予備発泡粒子を蒸
らす点にも本発明の特徴がある。水蒸気で予備発泡粒子
を蒸らす際には、予備加熱を行なった状態で行なっても
よく、また水蒸気の供給を停止し、さらに加えてドレイ
ン弁を開けた状態で行なってもよい。このように予備発
泡粒子を蒸らしたばあいには、成形型内の予備発泡粒子
間に導入された水蒸気の潜熱を有効に利用することがで
き、とくに厚さが大きい型内発泡体を作製するばあい、
予備発泡粒子を均一に加熱することができるという利点
がある。なお、予備発泡粒子をこのように蒸らすばあい
には、かかる蒸らしに要する時間は、成形型内における
予備発泡粒子層の厚さ、予備発泡粒子の大きさ、形状や
発泡倍率などによって水蒸気による熱伝達速度が異なる
ので一概には決定することができないが、通常予備発泡
粒子層の厚さがたとえば50mm程度のもので約３秒間以
上、好ましくは約５秒間以上、より好ましくは10秒間以
上とすることが望ましい。Another feature of the present invention is that steam is supplied from the steam holes 4 of the mold B2 for preheating and then the pre-expanded particles are steamed with steam. When the pre-expanded particles are steamed with steam, the pre-heated particles may be steamed, or the steam supply may be stopped and the drain valve may be opened. When the pre-expanded particles are steamed in this way, the latent heat of the steam introduced between the pre-expanded particles in the molding die can be effectively utilized, and an in-mold foam having a particularly large thickness is produced. Bad,
There is an advantage that the pre-expanded particles can be heated uniformly. When steaming the pre-expanded particles in this way, the time required for such steaming depends on the thickness of the pre-expanded particle layer in the molding die, the size of the pre-expanded particles, the shape, the expansion ratio, etc. Although it cannot be unconditionally determined because the transmission speed is different, it is usually about 3 seconds or more, preferably about 5 seconds or more, more preferably 10 seconds or more when the thickness of the pre-expanded particle layer is about 50 mm. Is desirable.
【００２９】前記蒸らしを行なった後には、予備発泡粒
子間にドレイン（水分）が存在し、その状態で本加熱を
行なえば、予備発泡粒子同士の融着不良が生じるため、
蒸らしで生じたドレインを除去することが好ましい。か
かるドレインを除去する方法としては、たとえば金型Ｂ
２に設けられた蒸気孔４を利用して成形室７内を真空引
きする方法、該蒸気孔４に予備発泡粒子が融着しない程
度の高温の乾燥した空気を通気させ、金型Ａ１と金型Ｂ
２との間に空隙を設け、かかる空隙からドレインを除去
する方法などがあげられるが、本発明はかかる方法によ
って限定されるものではない。After the steaming, there is a drain (water content) between the pre-expanded particles, and if main heating is performed in that state, defective fusion between the pre-expanded particles will occur.
It is preferable to remove the drain generated by steaming. As a method of removing such a drain, for example, a mold B is used.
2. A method of evacuating the inside of the molding chamber 7 by utilizing the steam holes 4 provided in 2; a high-temperature dry air that does not cause the pre-expanded particles to be fused is ventilated through the steam holes 4, and the mold A1 and the metal Type B
There is a method of providing a space between the space and the drain and removing the drain from the space, but the present invention is not limited to such a method.
【００３０】つぎに、前記予備発泡粒子がたがいに融着
する温度以上の温度で該予備発泡粒子を本加熱する。Next, the pre-expanded particles are subjected to main heating at a temperature equal to or higher than the temperature at which the pre-expanded particles are fused with each other.
【００３１】かかる本加熱は、金型Ｂ２の蒸気孔４から
水蒸気を通じることにより行なうことができる。The main heating can be performed by passing steam through the steam holes 4 of the mold B2.
【００３２】前記水蒸気の圧力は、水蒸気の温度が後述
する温度範囲内となるように調整すればよい。The pressure of the steam may be adjusted so that the temperature of the steam falls within the temperature range described later.
【００３３】前記水蒸気の温度は、予備発泡粒子がたが
いに融着する温度以上であればよいが、あまりにも該水
蒸気の温度が高すぎるばあいには、えられる型内発泡成
形体の収縮が大きくなりすぎる傾向があるので、該予備
発泡粒子が融着する温度よりも30℃高い温度以下、好ま
しくは該予備発泡粒子が融着する温度よりも25℃高い温
度以下とすることが望ましい。The temperature of the steam may be higher than the temperature at which the pre-expanded particles are fused with each other. However, if the temperature of the steam is too high, shrinkage of the obtained in-mold foamed molded product may occur. Since it tends to become too large, it is desirable that the temperature is 30 ° C. or higher than the temperature at which the pre-expanded particles are fused, and preferably 25 ° C. or higher than the temperature at which the pre-expanded particles are fused.
【００３４】前記予備発泡粒子を本加熱後、予備発泡粒
子に水蒸気による熱を充分に伝達するために、その状態
を保持することが好ましい。かかる保持に要する時間
は、予備発泡粒子層の厚さなどによって異なるので一概
には決定することができないが、一例としてたとえば予
備発泡粒子層の厚さが50mm程度のものに対しては約２秒
間以上、好ましくは約５秒間以上であることが望ましい
が、あまりにもその時間が長すぎるばあいには、えられ
る型内発泡成形体に収縮が生じるので、成形の際に収縮
が発生しない範囲内で適宜設定することが好ましい。After the pre-expanded particles have been main-heated, it is preferable that the pre-expanded particles be kept in that state in order to sufficiently transfer the heat of the steam to the pre-expanded particles. The time required for such holding varies depending on the thickness of the pre-expanded particle layer, etc., and therefore cannot be unconditionally determined, but for example, for a pre-expanded particle layer having a thickness of about 50 mm, it takes about 2 seconds. Above, preferably about 5 seconds or more is desirable, but if the time is too long, shrinkage will occur in the obtained in-mold foam molded article, so within the range where shrinkage does not occur during molding. It is preferable to set it appropriately.
【００３５】つぎに成形型を型開きすることにより、型
内発泡成形体がえられる。Then, the molding die is opened to obtain an in-mold foam molding.
【００３６】なお、本発明においては、成形型を型開き
する前に、えられた型内発泡成形体をあらかじめ冷却し
ておいてもよい。In the present invention, the obtained in-mold foamed molded product may be cooled in advance before the mold is opened.
【００３７】また、えられた型内発泡成形体は、成形型
から離脱したあとに、たとえば50〜80℃の常圧下で３〜
24時間程度養生、乾燥することが好ましい。Further, the obtained in-mold foamed molded product, after being separated from the molding mold, has a temperature of 3 to 3 at normal pressure of 50 to 80 ° C., for example.
It is preferable to cure and dry for about 24 hours.
【００３８】本発明のオレフィン系樹脂型内発泡成形体
の製造法によれば、蒸気孔を有しない金型面においても
予備発泡粒子の融着不良の発生がない型内発泡成形体を
製造することができる。According to the method for producing an in-mold foamed molded product of an olefinic resin of the present invention, an in-mold foamed molded product in which the pre-foamed particles do not fuse poorly even on a mold surface having no steam holes is manufactured. be able to.
【００３９】本発明の製造法は、また成形型において２
面の金型の蒸気孔による両面加熱を適用することができ
ない肉厚が大きい型内発泡体を成形したばあいであって
も、予備発泡粒子の融着不良を起こすことなく、良好な
型内発泡成形体を提供しうるので、とくに型内発泡体の
肉厚が比較的大きい、たとえば該肉厚が200 mm程度と大
きい型内発泡成形体をも好適に製造することができる。The manufacturing method of the present invention is also used in the molding die.
Even if you are molding an in-mold foam with a large wall thickness that cannot apply double-sided heating due to the steam holes of the mold on the surface, it does not cause defective fusion of the pre-expanded particles and Since it is possible to provide a foamed molded product, it is possible to preferably manufacture an in-mold foamed molded product having a relatively large wall thickness of the in-mold foamed product, for example, a large wall thickness of about 200 mm.
【００４０】つぎに本発明のオレフィン系樹脂型内発泡
成形体の製造法を実施例に基づいてさらに詳細に説明す
るが、本発明はかかる実施例のみに限定されるものでは
ない。Next, the method for producing the olefin resin in-mold foamed article of the present invention will be described in more detail based on examples, but the present invention is not limited to these examples.
【００４１】実施例１ 蒸気孔を有しない平板状の金型Ａと、蒸気孔を有する金
型Ｂ（成形室の寸法：たて300 mm、よこ300 mm、奥行50
mm）とを型締めして構成された成形型を用意した。Example 1 A flat plate-shaped mold A having no steam holes and a mold B having steam holes (dimensions of molding chamber: vertical 300 mm, width 300 mm, depth 50)
mm) and a mold were prepared.
【００４２】オレフィン系樹脂予備発泡粒子としてポリ
プロピレン系樹脂予備発泡粒子エペランＰＰ（鐘淵化学
工業（株）製、商品名、発泡倍率45倍）をあらかじめ耐
圧容器内に入れて空気圧で内圧２kg／cm2 ・G が付与さ
れたものを用い、これを金型Ｂに設けられたフィーダー
を介して成形型の成形室内に充填した。Polyolefin resin pre-expanded particles as olefin resin pre-expanded particles Eperan PP (manufactured by Kaneka Chemical Industry Co., Ltd., trade name, foaming ratio 45 times) was put in a pressure resistant container in advance and the internal pressure was 2 kg / cm by air pressure. Using the one to which 2 · G was added, this was filled into the molding chamber of the molding die through the feeder provided in the mold B.
【００４３】つぎに金型Ｂの蒸気孔から水蒸気（蒸気圧
0.5 kg／cm2 ・G 、温度109 〜113℃）を成形室内に導
入して予備加熱をし、10秒間予備発泡粒子の蒸らしを行
なったのち、成形室内の内圧が500mmHg 以下となるよう
に真空ポンプを用いてドレインおよび水蒸気を吸引し、
除去した。Next, steam (vapor pressure) is passed through the steam holes of the mold B.
0.5 kg / cm 2 · G, temperature 109-113 ° C) is introduced into the molding chamber and preheated to steam the pre-expanded particles for 10 seconds, and then vacuum is applied so that the internal pressure in the molding chamber is 500 mmHg or less. Use a pump to draw drain and water vapor,
Removed.
【００４４】そののち、金型Ｂの蒸気孔から水蒸気（蒸
気圧2.4 〜2.8 kg／cm2 ・G 、温度137 〜142 ℃）を成
形室内に導入し、25秒間保持したのち、水冷し、ついで
金型Ａと金型Ｂとを型開きしてオレフィン系樹脂型内発
泡成形体をえた。After that, steam (vapor pressure 2.4 to 2.8 kg / cm 2 · G, temperature 137 to 142 ° C.) was introduced into the molding chamber from the steam holes of the mold B, kept for 25 seconds, cooled with water, and then cooled. The mold A and the mold B were opened to obtain an olefin resin in-mold foam molded product.
【００４５】えられた型内発泡成形体の物性として、融
着率および表面状態を以下の方法にしたがって調べた。
その結果を表１に示す。As the physical properties of the obtained in-mold foamed molded product, the fusion rate and the surface condition were examined according to the following methods.
The results are shown in Table 1.
【００４６】（イ）融着率 えられた型内発泡成形体の表面にナイフで薄く切れ目を
入れたのち、折り曲げて破断させ、その破断面を観察
し、発泡粒子の破断面積の割合を百分率で表わし、以下
の評価基準に基づいて評価した。(A) Fusing rate After making a thin cut on the surface of the obtained in-mold foamed molded product with a knife, it was bent and broken, and the broken surface was observed, and the broken area ratio of the foamed particles was expressed as a percentage. And evaluated based on the following evaluation criteria.
【００４７】（評価基準） Ａ：融着率が60％以上 Ｂ：融着率が40〜59％ Ｃ：融着率が20〜39％ Ｄ：融着率が19％以下 （ロ）表面状態 えられた型内発泡成形体の蒸気孔が設けられていない金
型面における表面状態を目視により観察し、以下の評価
基準に基づいて評価した。(Evaluation Criteria) A: The fusion rate is 60% or more B: The fusion rate is 40 to 59% C: The fusion rate is 20 to 39% D: The fusion rate is 19% or less (b) Surface condition The surface state of the obtained mold surface of the in-mold foamed product on which the steam holes were not provided was visually observed and evaluated based on the following evaluation criteria.
【００４８】（評価基準） Ａ：予備発泡粒子同士が充分に融着し、その表面が平滑
である。(Evaluation Criteria) A: The pre-expanded particles are sufficiently fused with each other and the surface thereof is smooth.
【００４９】Ｂ：予備発泡粒子同士の融着が充分である
が、その表面はやや平滑さに欠ける。B: Sufficient fusion between the pre-expanded particles, but the surface thereof was slightly lacking in smoothness.
【００５０】Ｃ：予備発泡粒子同士の融着が充分でない
部分があり、その表面が平滑でない。C: There is a portion where the pre-expanded particles are not sufficiently fused, and the surface is not smooth.
【００５１】Ｄ：予備発泡粒子同士の融着が充分でない
部分が明らかに認められる。D: A portion where the pre-expanded particles are not sufficiently fused to each other is clearly recognized.
【００５２】実施例２ 実施例１で用いたのと同じ成形型を用いた。Example 2 The same mold used in Example 1 was used.
【００５３】オレフィン系樹脂予備発泡粒子としてポリ
プロピレン系樹脂予備発泡粒子エペランＰＰ（鐘淵化学
工業（株）製、商品名、発泡倍率30倍）を金型Ｂに設け
られたフィーダーを介して成形室内に充填した。Polyolefin resin pre-expanded particles as olefin resin pre-expanded particles Eperan PP (manufactured by Kanegafuchi Chemical Industry Co., Ltd., trade name, foaming ratio 30 times) is placed in a molding chamber through a feeder provided in a mold B. Filled.
【００５４】つぎに金型Ｂの蒸気孔から水蒸気（蒸気圧
0.5 kg／cm2 ・G 、温度109 〜113℃）を成形室内に導
入して予備加熱をし、除圧して10秒間予備発泡粒子の蒸
らしを行なったのち、成形室内の内圧が260mmHg 以下と
なるように真空ポンプを用いてドレインおよび水蒸気を
吸引し、除去した。Next, steam (vapor pressure) is passed through the steam holes of the mold B.
0.5 kg / cm 2 · G, temperature 109-113 ℃) is introduced into the molding chamber to preheat, depressurize and steam the pre-expanded particles for 10 seconds, and then the internal pressure in the molding chamber becomes 260 mmHg or less. Thus, the drain and water vapor were sucked and removed using the vacuum pump.
【００５５】そののち、金型Ｂの蒸気孔から水蒸気（蒸
気圧3.2 kg／cm2 ・G 、温度144 〜146 ℃）を成形室内
に導入し、20秒間保持したのち、冷却し、ついで金型Ａ
と金型Ｂとを型開きしてオレフィン系樹脂型内発泡成形
体をえた。After that, steam (vapor pressure: 3.2 kg / cm 2 · G, temperature: 144 to 146 ° C.) was introduced into the molding chamber through the steam holes of the mold B, kept for 20 seconds, cooled, and then the mold. A
The mold B was opened to obtain an olefin resin in-mold foam molded product.
【００５６】えられた型内発泡成形体の物性を実施例１
と同様にして調べた。その結果を表１に示す。The physical properties of the obtained in-mold foamed molded product are shown in Example 1.
I examined it in the same way. The results are shown in Table 1.
【００５７】実施例３ 蒸気孔を有しない平板状の金型Ａと、蒸気孔を有する金
型Ｂ（成形室の寸法：たて300 mm、よこ300 mm、奥行20
0 mm）とを型締めして構成された成形型を用意した。Example 3 A flat plate-shaped mold A having no steam holes and a mold B having steam holes (dimensions of molding chamber: vertical 300 mm, horizontal 300 mm, depth 20)
0 mm) and a mold were prepared.
【００５８】実施例２において、オレフィン系樹脂予備
発泡粒子としてポリプロピレン系樹脂予備発泡粒子エペ
ランＰＰ（鐘淵化学工業（株）製、商品名、発泡倍率15
倍）を用い、金型Ｂの蒸気孔から水蒸気（蒸気圧1.0 kg
／cm2 ・G 、温度117 〜123℃）を成形室内に導入して
予備加熱をし、除圧して20秒間予備発泡粒子の蒸らしを
行なったほかは、実施例２と同様にして予備発泡粒子の
充填からドレインおよび水蒸気の吸引除去までを行なっ
た。In Example 2, as the olefin resin pre-expanded particles, polypropylene resin pre-expanded particles Eperan PP (manufactured by Kaneka Chemical Co., Ltd., trade name, expansion ratio 15
From the steam holes of mold B (steam pressure 1.0 kg)
/ Cm 2 · G, temperature 117-123 ° C) was introduced into the molding chamber to preheat, depressurize and steam the prefoamed particles for 20 seconds, and the prefoamed particles were the same as in Example 2. From filling of the drain to suction removal of water vapor.
【００５９】つぎに金型Ｂの蒸気孔から水蒸気（蒸気圧
3.5 〜3.8 kg／cm2 ・G 、温度147〜151 ℃）を成形室
内に導入し、25秒間保持したのち、冷却し、ついで金型
Ａと金型Ｂとを型開きしてオレフィン系樹脂型内発泡成
形体をえた。Next, steam (vapor pressure) is passed through the steam holes of the mold B.
(3.5 to 3.8 kg / cm 2 · G, temperature 147 to 151 ℃) is introduced into the molding chamber, held for 25 seconds, cooled, and then mold A and mold B are opened to open the olefin resin mold. An inner foam molding was obtained.
【００６０】えられた型内発泡成形体の物性を実施例１
と同様にして調べた。その結果を表１に示す。The physical properties of the obtained in-mold foamed molded product are shown in Example 1.
I examined it in the same way. The results are shown in Table 1.
【００６１】比較例１ 実施例１において、予備加熱後、蒸らしを行なわずにド
レインおよび水蒸気の吸引除去を行なったほかは、実施
例１と同様にしてオレフィン系樹脂型内発泡成形体をえ
た。Comparative Example 1 An olefin resin in-mold foam molded article was obtained in the same manner as in Example 1, except that after preheating, the drain and water vapor were removed by suction without steaming.
【００６２】えられた型内発泡成形体の物性を実施例１
と同様にして調べた。その結果を表１に示す。The physical properties of the obtained in-mold foamed molded product are shown in Example 1.
I examined it in the same way. The results are shown in Table 1.
【００６３】比較例２ 実施例２において、予備加熱後に蒸らしを行なわなかっ
たほかは、実施例２と同様にしてオレフィン系樹脂型内
発泡成形体をえた。Comparative Example 2 An olefin resin in-mold foam molded article was obtained in the same manner as in Example 2 except that steaming was not performed after preheating.
【００６４】えられた型内発泡成形体の物性を実施例１
と同様にして調べた。その結果を表１に示す。The physical properties of the obtained in-mold foamed molded product are shown in Example 1.
I examined it in the same way. The results are shown in Table 1.
【００６５】[0065]
【表１】 [Table 1]
【００６６】表１に示した結果から明らかなように、本
発明の実施例１〜３のオレフィン系樹脂型内発泡成形体
の製造法によれば、蒸気孔を有しない金型面においても
予備発泡粒子の融着不良の発生がなく、平滑でかつ美麗
な表面を有するオレフィン系樹脂型内発泡成形体を作製
することができることがわかる。As is clear from the results shown in Table 1, according to the method for producing the olefin resin in-mold foamed molded articles of Examples 1 to 3 of the present invention, even on the die surface having no vapor holes, preliminary It can be seen that it is possible to produce an olefin-based resin in-mold foam molded article having a smooth and beautiful surface without causing defective fusion of the foamed particles.
【００６７】[0067]
【発明の効果】本発明のオレフィン系樹脂型内発泡成形
体の製造法によれば、蒸気孔を有しない金型を用い、該
金型面から予備発泡粒子の蒸気加熱が行なわれないばあ
いであっても、蒸気孔を有しない金型面で予備発泡粒子
の融着不良などの発生などがない外観が美麗な型内発泡
成形体を提供しうるすぐれた効果が奏せられる。According to the method for producing an olefin resin in-mold foam molded article of the present invention, when a die having no vapor holes is used and the pre-expanded particles are not heated by vapor from the die surface. Even in this case, there is an excellent effect that it is possible to provide an in-mold foamed molded article having a beautiful appearance, which does not cause defective fusion of the pre-foamed particles on the mold surface having no steam holes.
【図１】本発明の製造法に用いられる成形型の一実施態
様を示す概略説明図である。FIG. 1 is a schematic explanatory view showing one embodiment of a molding die used in the production method of the present invention.
１ 蒸気孔を有しない金型Ａ ２ 蒸気孔を有する金型Ｂ ４ 蒸気孔 1 Mold A without Steam Holes A 2 Mold with Steam Holes B 4 Steam Holes
Claims (2)
る金型Ｂとを型締めして成形型を構成したのち、オレフ
ィン系樹脂予備発泡粒子を該成形型内に充填し、金型Ｂ
の蒸気孔から水蒸気を供給し、該予備発泡粒子がたがい
に融着する温度よりも低い温度で該予備発泡粒子を予備
加熱し、該予備発泡粒子を水蒸気で蒸らし、ついで該予
備発泡粒子がたがいに融着する温度以上の温度で該予備
発泡粒子を本加熱することを特徴とするオレフィン系樹
脂型内発泡成形体の製造法。1. A mold is formed by clamping a mold A having no steam holes and a mold B having steam holes, and then pre-expanded olefin resin particles are filled in the mold to obtain a metal mold. Type B
Water vapor is supplied from the vapor holes of the pre-expanded particles, the pre-expanded particles are pre-heated at a temperature lower than the temperature at which the pre-expanded particles are fused to each other, the pre-expanded particles are steamed with steam, and then the pre-expanded particles are followed. A method for producing an olefin-based resin in-mold expansion-molded article, characterized in that the pre-expanded particles are permanently heated at a temperature equal to or higher than the temperature at which they are fused to each other.
したのちに本加熱をする請求項１記載のオレフィン系樹
脂型内発泡成形体の製造法。2. The method for producing an olefin-based resin in-mold foam molded article according to claim 1, wherein the pre-expanded particles are steamed, the drain is removed, and then the main heating is performed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP05012314A JP3081722B2 (en) | 1992-06-04 | 1993-01-28 | Method for producing foamed molded article in olefin resin mold |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4-144311 | 1992-06-04 | ||
| JP14431192 | 1992-06-04 | ||
| JP05012314A JP3081722B2 (en) | 1992-06-04 | 1993-01-28 | Method for producing foamed molded article in olefin resin mold |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0647829A true JPH0647829A (en) | 1994-02-22 |
| JP3081722B2 JP3081722B2 (en) | 2000-08-28 |
Family
ID=26347896
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP05012314A Expired - Fee Related JP3081722B2 (en) | 1992-06-04 | 1993-01-28 | Method for producing foamed molded article in olefin resin mold |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3081722B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000246849A (en) * | 1999-02-26 | 2000-09-12 | Nishikawa Kasei Co Ltd | Resin molding and its manufacture |
| JP2005088442A (en) * | 2003-09-18 | 2005-04-07 | Kaneka Corp | Method for manufacturing in-mold foam molded body of thermoplastic resin and molded body |
-
1993
- 1993-01-28 JP JP05012314A patent/JP3081722B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000246849A (en) * | 1999-02-26 | 2000-09-12 | Nishikawa Kasei Co Ltd | Resin molding and its manufacture |
| JP2005088442A (en) * | 2003-09-18 | 2005-04-07 | Kaneka Corp | Method for manufacturing in-mold foam molded body of thermoplastic resin and molded body |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3081722B2 (en) | 2000-08-28 |
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