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JP2686509B2 - Method for producing composite foam - Google Patents

Method for producing composite foam

Info

Publication number
JP2686509B2
JP2686509B2 JP30180388A JP30180388A JP2686509B2 JP 2686509 B2 JP2686509 B2 JP 2686509B2 JP 30180388 A JP30180388 A JP 30180388A JP 30180388 A JP30180388 A JP 30180388A JP 2686509 B2 JP2686509 B2 JP 2686509B2
Authority
JP
Japan
Prior art keywords
resin
foam
particles
thermoplastic resin
composite foam
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.)
Expired - Lifetime
Application number
JP30180388A
Other languages
Japanese (ja)
Other versions
JPH02147219A (en
Inventor
博之 穐山
英樹 桑原
和男 鶴飼
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.)
JSP Corp
Original Assignee
JSP Corp
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 JSP Corp filed Critical JSP Corp
Priority to JP30180388A priority Critical patent/JP2686509B2/en
Publication of JPH02147219A publication Critical patent/JPH02147219A/en
Application granted granted Critical
Publication of JP2686509B2 publication Critical patent/JP2686509B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は複合発泡体の製造方法に関する。TECHNICAL FIELD The present invention relates to a method for producing a composite foam.

〔従来の技術及び発明が解決しようとする課題〕[Problems to be solved by conventional technology and invention]

近年、断熱材、緩衝材、浮揚材等に合成樹脂発泡成型
体が広く用いられており、この種の発泡成型体を製造す
る方法としては、合成樹脂予備発泡粒子を所望の形状の
成型用型内に充填した後、加熱して該予備発泡粒子を発
泡せしめ型通りの成型体を得るいわゆるビーズ成型法が
知られている。ビーズ成型法は独立気泡率の高い発泡成
型体を得やすく、断熱性、耐水性等に優れた発泡成型体
を得るための方法として好ましいものであるが、反面高
発泡倍率の成型体では発泡成型体が収縮しやすく、寸法
精度の高い成型体を得るためには高度の技術を必要と
し、そうでない場合には表面平滑性に難点を生じ易い。
また成型に当って成型用型内で予備発泡粒子を加熱した
後冷却する工程をくり返して行なうものであるため、成
型のたびに成型用型加熱に要する熱エネルギーを損失
し、しかも一回の成型に要する時間が長く、従って成型
のサイクルが長くなりその結果熱効率、成型効率が低い
という欠点を有していた。一方、射出成型法は成型用型
を樹脂の融点近傍またはそれ以上迄加熱する必要がない
ため、射出成型法を用いれば、一般には熱効率、成型効
率を向上できるが、未発泡の合成樹脂(例えば合成樹脂
ペレット)から発泡成型を行なって成型体を得る従来の
射出成型法では1.5倍程度の発泡倍率の成型体しか得ら
れず、より高い発泡倍率(低密度)の成型体を得る方法
の開発が求められていた。
2. Description of the Related Art In recent years, synthetic resin foam molded articles have been widely used as heat insulating materials, cushioning materials, floating materials, and the like. As a method for producing this type of foam molded article, synthetic resin pre-expanded particles are molded into a mold having a desired shape. A so-called bead molding method is known in which the pre-expanded particles are heated after being filled in the inside thereof to form a molded product according to a mold. The bead molding method is preferable as a method for easily obtaining a foamed molded product having a high closed cell ratio and excellent heat insulation and water resistance, but on the other hand, a foamed molded product having a high expansion ratio is foamed molded. The body tends to shrink, and a high degree of technology is required to obtain a molded body with high dimensional accuracy, and if it is not the case, the surface smoothness tends to be difficult.
In addition, since the process of heating the pre-expanded particles in the molding die and then cooling is repeated during molding, the heat energy required for heating the molding die is lost each time molding is performed, and moreover, once molding is performed. It takes a long time to complete the molding process, resulting in a long molding cycle, resulting in low thermal efficiency and low molding efficiency. On the other hand, in the injection molding method, since it is not necessary to heat the molding die to a temperature close to or above the melting point of the resin, the injection molding method can generally improve the thermal efficiency and molding efficiency. Development of a method to obtain a molded product with a higher expansion ratio (low density), because only a molded product with an expansion ratio of about 1.5 times can be obtained with the conventional injection molding method in which foamed molding is performed from synthetic resin pellets) Was required.

上記の問題点を解決するため本発明者は合成樹脂発泡
粒子を加熱軟化せしめた後、成型用型内に加圧して射出
し成型する方法を提案した(特開昭60−96419号)。こ
の方法によれば従来の射出発泡法に比べて高発泡の発泡
形成品を容易に得ることができるが、この方法では得ら
れる成型品の発泡倍率が発泡粒子の溶融度合で変化して
しまい所望の発泡倍率の成型品を得ることが困難である
という問題があった。これはわずかな温度変化によって
発泡粒子の溶融度合が大きく変化することに起因し、こ
のような傾向はポリオレフィン系樹脂のごとく高結晶性
樹脂よりなる発泡粒子ではいっそう顕著となり、成型体
における発泡粒子相互の融着強度の低下をきたしやす
く、樹脂によってはほとんど融着が行なわれない場合が
ある等の問題を有し、改良の余地が残されていた。
In order to solve the above problems, the present inventor has proposed a method of heating and softening synthetic resin foamed particles, and then pressurizing and injecting them into a mold for molding (JP-A-60-96419). According to this method, a foamed product having high foaming can be easily obtained as compared with the conventional injection foaming method. However, according to this method, the expansion ratio of the obtained molded product changes depending on the degree of melting of the foamed particles, and thus the desired value is obtained. There is a problem that it is difficult to obtain a molded product having the expansion ratio of This is due to the fact that the degree of melting of the foamed particles greatly changes with a slight temperature change, and such a tendency becomes more remarkable in the foamed particles made of a highly crystalline resin such as a polyolefin resin, and the mutual expansion of the foamed particles in the molded body is caused. However, there is a problem in that the fusion strength of the resin is likely to be lowered, and the fusion may not be performed depending on the resin. Therefore, there is room for improvement.

〔課題を解決するための手段〕[Means for solving the problem]

本発明は上記課題を解決するためになされたもので、
従来技術の欠点を解消し得る複合発泡体の製造方法を提
供することを目的とする。
The present invention has been made to solve the above problems,
An object of the present invention is to provide a method for producing a composite foam which can solve the disadvantages of the prior art.

即ち本発明は、 (1) 射出成型用型内に熱可塑性発泡粒子又はその複
数結合体を装填し、次いで該型内に熱可塑性樹脂を射出
して熱可塑性樹脂と熱可塑性樹脂発泡粒子とが一体化し
た複合体を得ることを特徴とする複合発泡体の製造方
法。
That is, the present invention provides (1) loading thermoplastic foam particles or a plurality of combinations thereof into an injection molding mold, and then injecting a thermoplastic resin into the mold to obtain a thermoplastic resin and thermoplastic resin foam particles. A method for producing a composite foam, which comprises obtaining an integrated composite.

(2) 熱可塑性樹脂発泡粒子の密度が0.3〜0.015g/cm
3であることを特徴とする請求項1記載の複合発泡体の
製造方法。
(2) Thermoplastic resin expanded particles have a density of 0.3 to 0.015 g / cm
3. The method for producing a composite foam according to claim 1, wherein the number is 3 .

(3) 熱可塑性樹脂発泡粒子がポリオレフィン系樹脂
発泡粒子であることを特徴とする請求項1又は2記載の
複合発泡体の製造方法。
(3) The method for producing a composite foam according to claim 1 or 2, wherein the expanded thermoplastic resin particles are expanded polyolefin resin particles.

(4) ポリオレフィン系樹脂発泡粒子が無架橋ポリプ
ロピレン系樹脂発泡体、無架橋直鎖状低密度ポリエチレ
ン系樹脂発泡体、架橋ポリエチレン系樹脂発泡体、架橋
ポリプロピレン系樹脂発泡体のいずれかであることを特
徴とする請求項3記載の複合発泡体の製造方法。
(4) The polyolefin resin foam particles are any of a non-crosslinked polypropylene resin foam, a non-crosslinked linear low-density polyethylene resin foam, a crosslinked polyethylene resin foam, and a crosslinked polypropylene resin foam. The method for producing a composite foam according to claim 3, which is characterized in that.

を要旨とするものである。It is the gist.

本発明方法は第1図に示すように射出成型用金型1内
に充填口2から熱可塑性樹脂発泡粒子3を供給して型内
に充填した後、第2図に示すようにピストン4によって
充填口2を塞ぎ、次いで射出機5から熱可塑性樹脂6を
射出して発泡粒子3と射出した熱可塑性樹脂6とを一体
化するものであり、上記発泡粒子3としては独立気泡構
造の熱可塑性樹脂発泡粒子を用いることが好ましい。発
泡粒子3は独立気泡率80%以上のものが好ましく、発泡
粒子3の独立気泡率が低いと、射出された溶融樹脂によ
って発泡粒子の表面が加熱され、二次発泡、破泡、収縮
等を生じ易くなる。発泡粒子3としては高密度ポリエチ
レン、中密度ポリエチレン、低密度ポリエチレン、直鎖
状低密度ポリエチレン、直鎖状超低密度ポリエチレン、
ポリプロピレン、エチレン−プロピレン共重合体、エチ
レン−酢酸ビニル共重合体等のポリオレフィン系樹脂、
ポリスチレン、ポリ−α−スチレン、スチレン−無水マ
レイン酸共重合体等のポリスチレン系樹脂、ポリ塩化ビ
ニル系樹脂、ポリ塩化ビニリデン系樹脂、ナイロン、芳
香族ナイロン等のポリアミド系樹脂、ポリエチレンテレ
フタレート、ポリブチレンテレフタレート等のポリエス
テル系樹脂、ポリカーボネート系樹脂等の熱可塑性樹脂
よりなる発泡粒子を用いることができるが、特に架橋発
泡粒子、結晶性樹脂発泡粒子が射出成型機から射出され
た溶融流動する高温の樹脂の影響を受けて発泡粒子が溶
融等の変化をきたし難い点で好ましく、なかでも無架橋
ポリプロピレン系樹脂発泡粒子、無架橋直鎖状低密度ポ
リエチレン系樹脂発泡粒子、架橋ポリエチレン系樹脂発
泡粒子、架橋ポリプロピレン系樹脂発泡粒子が好ましい
が、特に好ましいのは架橋ポリエチレン系樹脂発泡粒
子、架橋ポリプロピレン系樹脂発泡粒子である。また発
泡粒子3としては密度0.3〜0.015g/cm3のものが、適当
な弾性と耐熱性を有し好ましい。
According to the method of the present invention, as shown in FIG. 1, the thermoplastic resin foam particles 3 are supplied from the filling port 2 into the injection molding die 1 to fill the inside of the die, and then, as shown in FIG. The filling port 2 is closed, and then the thermoplastic resin 6 is injected from the injection machine 5 to integrate the expanded particles 3 and the injected thermoplastic resin 6, and the expanded particles 3 have a closed-cell structure of thermoplasticity. It is preferable to use resin expanded particles. The foamed particles 3 preferably have a closed cell ratio of 80% or more. When the closed cell ratio of the foamed particles 3 is low, the surface of the foamed particles is heated by the injected molten resin, and secondary foaming, breakage, shrinkage, etc. occur. It tends to occur. As the foamed particles 3, high density polyethylene, medium density polyethylene, low density polyethylene, linear low density polyethylene, linear ultra low density polyethylene,
Polyolefin resin such as polypropylene, ethylene-propylene copolymer, ethylene-vinyl acetate copolymer,
Polystyrene resin such as polystyrene, poly-α-styrene, styrene-maleic anhydride copolymer, polyvinyl chloride resin, polyvinylidene chloride resin, nylon, polyamide resin such as aromatic nylon, polyethylene terephthalate, polybutylene Polyethylene resin such as terephthalate, foamed particles made of thermoplastic resin such as polycarbonate resin can be used, but in particular crosslinked foamed particles, crystalline resin foamed particles are melt-flowing high temperature resin injected from an injection molding machine. Is preferable in that the expanded particles are less likely to undergo changes such as melting under the influence of, among others, non-crosslinked polypropylene resin expanded particles, non-crosslinked linear low-density polyethylene resin expanded particles, crosslinked polyethylene resin expanded particles, crosslinked Polypropylene resin foamed particles are preferred, but particularly preferred The crosslinked polyethylene resin foamed beads, cross-linked polypropylene resin foam particles. As the foamed particles 3, those having a density of 0.3 to 0.015 g / cm 3 are preferable because they have appropriate elasticity and heat resistance.

射出機5から射出する熱可塑性樹脂6としては前記発
泡粒子3を構成する樹脂と同様の樹脂の他に、ポリアセ
タール系樹脂、ポリフェニレンオキサイド系樹脂、ポリ
フェニレンサルファイド系樹脂、ポリフルフォン系樹
脂、ポリウレタン系樹脂、ABS系樹脂等の樹脂も用いる
ことができる。これらの樹脂は溶融粘度が低く、発泡粒
子又は発泡粒子結合体間に容易に流入するものが好まし
い。またこれらの樹脂中には必要に応じて発泡剤を含有
せしめておいても良く、発泡剤を含有せしめておくとヒ
ケの発生防止に役立つとともに、全体の重量増加の防止
を図れる。発泡剤としてはアゾジカルボンアミド、ジニ
トロソペンタメチレンテトラミン、アゾビスイソブチロ
ニトリル、重炭酸ナトリウム等が挙げられ、発泡剤を含
有させる場合、その添加量は樹脂100重量部当たり、0.1
〜10重量部が好ましい。発泡粒子3は金型1内に充填し
た時に粒子間隙(熱可塑性樹脂6が射出されるスペー
ス)を有するように充填することが必要であるが、熱可
塑性樹脂6が射出されるスペースを有すれば発泡粒子3
を圧縮充填しても良い。しかしながら圧縮充填しない場
合には、型内容積の60%以上(発泡粒子の見掛け容積に
対して)となるように充填することが好ましく、60%未
満であると得られる複合発泡体中における熱可塑性樹脂
の割合が多くなり、射出する熱可塑性樹脂中に発泡剤を
含有させたとしても複合発泡体の重量増加をきたす虞れ
がある。
As the thermoplastic resin 6 injected from the injection machine 5, in addition to the resin similar to the resin forming the foamed particles 3, a polyacetal resin, a polyphenylene oxide resin, a polyphenylene sulfide resin, a polyfluphone resin, a polyurethane resin is used. Resins such as ABS resin and the like can also be used. It is preferable that these resins have a low melt viscosity and easily flow between the expanded particles or the expanded particle bonded body. If necessary, a foaming agent may be contained in these resins. If the foaming agent is contained, it is possible to prevent the occurrence of sink marks and prevent an increase in the total weight. Examples of the foaming agent include azodicarbonamide, dinitrosopentamethylenetetramine, azobisisobutyronitrile, sodium bicarbonate and the like, and when the foaming agent is contained, the addition amount thereof is 100 parts by weight of the resin and 0.1
-10 parts by weight is preferred. The foamed particles 3 need to be filled so as to have a particle gap (space in which the thermoplastic resin 6 is injected) when they are filled in the mold 1, but there is a space in which the thermoplastic resin 6 is injected. If foamed particles 3
May be compressed and filled. However, when compression filling is not carried out, it is preferable to fill it so as to be 60% or more (relative to the apparent volume of expanded particles) of the internal volume of the mold, and if it is less than 60%, the thermoplasticity in the resulting composite foam The proportion of the resin increases, and even if the blowing agent is contained in the injected thermoplastic resin, the weight of the composite foam may increase.

上記樹脂を射出する射出条件としては、射出圧力500
〜1500kg/cm2・G、射出速度0.2〜3m/秒、射出樹脂の温
度100〜250℃であるが、各樹脂の融点、溶融した樹脂の
溶融粘度−温度特性、線断応力−溶融粘度特性等を勘案
して決定する。また金型温度は30〜90℃が好ましい。樹
脂射出後冷却を行うが、この冷却時間は60〜300秒程度
が好ましい。
The injection conditions for injecting the above resin are injection pressure 500
~ 1500 kg / cm 2 · G, injection speed 0.2 ~ 3 m / sec, temperature of injection resin is 100 ~ 250 ℃, melting point of each resin, melt viscosity of molten resin-temperature characteristic, line breaking stress-melt viscosity characteristic Etc. are taken into consideration when deciding. The mold temperature is preferably 30 to 90 ° C. Cooling is performed after resin injection, and the cooling time is preferably about 60 to 300 seconds.

本発明においては第3図に示すように発泡粒子3の充
填口2が型1の上面側に設けられていても良い。また充
填口2は1つの型に1つに限らず、複数の充填口を備え
た型を用いても良い。
In the present invention, the filling port 2 for the expanded particles 3 may be provided on the upper surface side of the mold 1 as shown in FIG. Further, the number of the filling port 2 is not limited to one in one mold, and a mold having a plurality of filling ports may be used.

〔実施例〕〔Example〕

以下、実施例を挙げて本発明を更に詳細に説明する。 Hereinafter, the present invention will be described in more detail with reference to examples.

実施例1〜7 第1表に示す発泡粒子を、縦100mm×横100mm×高さ30
mmの、85℃に加熱された射出成型用金型内に、第1表に
示す充填率で充填し、次いで同表に示す射出条件で熱可
塑性樹脂を射出した後、200秒間冷却して型より取り出
した。得られた複合発泡体の性状を第2表に示す。
Examples 1 to 7 The foamed particles shown in Table 1 were used to measure length 100 mm x width 100 mm x height 30
mm in an injection molding die heated to 85 ° C. at a filling rate shown in Table 1, and then a thermoplastic resin is injected under the injection conditions shown in the same table, followed by cooling for 200 seconds. I took it out. Table 2 shows the properties of the obtained composite foam.

※1 充填率は型内容積に対する、型内に充填された発 泡粒子の見掛け体積で示した。 * 1 The filling rate is indicated by the apparent volume of foam particles filled in the mold with respect to the internal volume of the mold.

※2 発泡剤の添加量は、樹脂100重量部当たりに対す る重量部で示した。* 2 The amount of foaming agent added is shown in parts by weight per 100 parts by weight of resin.

※3 発泡体の変形の有無を観察し、以下の基準で評価 した。* 3 The presence or absence of deformation of the foam was observed and evaluated according to the following criteria.

○・・・変形が認められない。 ○: No deformation is observed.

×・・・変形が認められる。 X: Deformation is recognized.

※4 発泡体表面を観察し、以下の基準で評価した。* 4 The surface of the foam was observed and evaluated according to the following criteria.

○・・・表面が平滑である。 ○: The surface is smooth.

×・・・表面に発泡粒子の凹凸模様が残る。 X: An uneven pattern of foamed particles remains on the surface.

〔発明の効果〕〔The invention's effect〕

以上説明したように本発明方法によれば未発泡の合成
樹脂ペレットから発泡成型を行なう従来の射出成型法に
比べて、より低密度の成型体を容易に得ることができ
る。しかも本発明方法によれば成型体の密度は発泡粒子
と熱可塑性樹脂の容積比により容易に決定できるため得
られる成型体の密度を容易にコントロールすることがで
き、密度の違いによる種々の物性の成型体を容易に製造
することができ、更に本発明方法によって得られた成型
体は従来のものに比べて強度の高いものとなる。また本
発明は発泡粒子と無発泡樹脂との組み合わせによるもの
であり、その樹脂の種類を変えることができるので、架
橋ポリエチレンの発泡粒子と硬質のポリエステルとの組
み合わせや、比較的硬質のエチレン−プロピレン系樹脂
発泡体と軟質のエチレン−酢酸ビニル共重合体との組み
合わせ等を必要に応じ自由に選択することができる。ま
た従来の発泡射出成型法による場合は表面層にも気泡構
造があり、このため表面硬度が低く、摩擦によって容易
に表面層が破れ、気泡構造が露出することがあり、外観
も平滑なものを得ることが困難であった。しかしながら
本発明方法によれば、表面層を平滑にすることも、また
その表面層の厚さを変更することもできる。
As described above, according to the method of the present invention, a molded article having a lower density can be easily obtained as compared with the conventional injection molding method in which foam molding is performed from unfoamed synthetic resin pellets. Moreover, according to the method of the present invention, the density of the molded product can be easily determined by the volume ratio of the expanded particles and the thermoplastic resin, so that the density of the resulting molded product can be easily controlled, and various physical properties due to the difference in density can be obtained. The molded body can be easily manufactured, and the molded body obtained by the method of the present invention has higher strength than the conventional one. Further, the present invention is based on a combination of expanded particles and a non-expanded resin, and since the type of the resin can be changed, a combination of expanded particles of crosslinked polyethylene and a hard polyester, or a relatively hard ethylene-propylene resin is used. A combination of a resin foam and a soft ethylene-vinyl acetate copolymer can be freely selected as necessary. In addition, in the case of the conventional foaming injection molding method, the surface layer also has a cell structure, so that the surface hardness is low, the surface layer may be easily broken by friction, and the cell structure may be exposed. It was difficult to get. However, according to the method of the present invention, the surface layer can be smoothed or the thickness of the surface layer can be changed.

本発明方法では発泡粒子として密度0.3〜0.015g/cm3
のものを用いることにより、射出樹脂の温度が高い場合
でも発泡粒子の気泡が破れて連続気泡化したり、収縮や
密度上昇をきたす虞れがない。また本発明では発泡粒子
としてポリオレフィン発泡粒子を用いた場合に優れた複
合発泡体を得ることができるが、特にポリオレフィン発
泡粒子の内でも無架橋ポリプロピレン系樹脂発泡粒子、
無架橋直鎖状低密度ポリエチレン系樹脂発泡粒子、架橋
ポリエチレン系樹脂発泡粒子、架橋ポリルロピレン系樹
脂発泡粒子を用いると更に収縮性の少ない、表面状態の
良好な複合発泡体を得ることができる。
In the method of the present invention, the density of foamed particles is 0.3 to 0.015 g / cm 3.
Even if the temperature of the injection resin is high, there is no fear that the bubbles of the foamed particles will be broken and become continuous bubbles, or that the shrinkage and the density increase will occur even if the temperature of the injection resin is high. Further, in the present invention, it is possible to obtain an excellent composite foam when using the polyolefin foamed particles as the foamed particles, but especially among the polyolefin foamed particles, non-crosslinked polypropylene resin foamed particles,
By using non-crosslinked linear low-density polyethylene-based resin foamed particles, crosslinked polyethylene-based resin foamed particles, and crosslinked polypropylene-based resin foamed particles, it is possible to obtain a composite foam having less shrinkage and a good surface condition.

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

図面は本発明の一実施例を示し、第1図〜第2図は本発
明方法の工程を示す成型装置の縦断面略図、第3図は成
型装置の異なる態様を示す縦断面略図である。 1……射出成型用金型、3……発泡粒子、5……射出
機、6……熱可塑性樹脂
The drawings show one embodiment of the present invention. FIGS. 1 and 2 are schematic vertical sectional views of a molding apparatus showing steps of the method of the present invention, and FIG. 3 is a schematic vertical sectional view showing a different aspect of the molding apparatus. 1 ... Injection mold, 3 ... Expanded particles, 5 ... Injection machine, 6 ... Thermoplastic resin

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29K 105:24 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code Agency reference number FI Technical display location B29K 105: 24

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】射出成型用型内に熱可塑性発泡粒子又はそ
の複数結合体を装填し、次いで該型内に熱可塑性樹脂を
射出して熱可塑性樹脂と熱可塑性樹脂発泡粒子とが一体
化した複合体を得ることを特徴とする複合発泡体の製造
方法。
1. A thermoplastic resin foamed particle or a plurality of combinations thereof are loaded into an injection molding mold, and then a thermoplastic resin is injected into the mold to integrate the thermoplastic resin and the thermoplastic resin foamed particle. A method for producing a composite foam, which comprises obtaining a composite.
【請求項2】熱可塑性樹脂発泡粒子の密度が0.3〜0.015
g/cm3であることを特徴とする請求項1記載の複合発泡
体の製造方法。
2. The density of expanded thermoplastic resin particles is 0.3 to 0.015.
The method for producing a composite foam according to claim 1, wherein the composite foam is g / cm 3 .
【請求項3】熱可塑性樹脂発泡粒子がポリオレフィン系
樹脂発泡粒子であることを特徴とする請求項1又は2記
載の複合発泡体の製造方法。
3. The method for producing a composite foam according to claim 1, wherein the expanded thermoplastic resin particles are expanded polyolefin resin particles.
【請求項4】ポリオレフィン系樹脂発泡粒子が無架橋ポ
リプロピレン系樹脂発泡体、無架橋直鎖状低密度ポリエ
チレン系樹脂発泡体、架橋ポリエチレン系樹脂発泡体、
架橋ポリプロピレン系樹脂発泡体のいずれかであること
を特徴とする請求項3記載の複合発泡体の製造方法。
4. A foamed polyolefin resin particle is a non-crosslinked polypropylene resin foam, a non-crosslinked linear low-density polyethylene resin foam, a crosslinked polyethylene resin foam,
The method for producing a composite foam according to claim 3, wherein the composite foam is any one of crosslinked polypropylene resin foams.
JP30180388A 1988-11-29 1988-11-29 Method for producing composite foam Expired - Lifetime JP2686509B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30180388A JP2686509B2 (en) 1988-11-29 1988-11-29 Method for producing composite foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30180388A JP2686509B2 (en) 1988-11-29 1988-11-29 Method for producing composite foam

Publications (2)

Publication Number Publication Date
JPH02147219A JPH02147219A (en) 1990-06-06
JP2686509B2 true JP2686509B2 (en) 1997-12-08

Family

ID=17901355

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30180388A Expired - Lifetime JP2686509B2 (en) 1988-11-29 1988-11-29 Method for producing composite foam

Country Status (1)

Country Link
JP (1) JP2686509B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006015440A1 (en) * 2004-08-12 2006-02-16 Pacific Strategies Consultants Pty Ltd Method of forming a composite material

Also Published As

Publication number Publication date
JPH02147219A (en) 1990-06-06

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