JPS5991039A - Manufacture of foamed and molded item - Google Patents

Manufacture of foamed and molded item

Info

Publication number
JPS5991039A
JPS5991039A JP57202589A JP20258982A JPS5991039A JP S5991039 A JPS5991039 A JP S5991039A JP 57202589 A JP57202589 A JP 57202589A JP 20258982 A JP20258982 A JP 20258982A JP S5991039 A JPS5991039 A JP S5991039A
Authority
JP
Japan
Prior art keywords
gas
molding
foaming
foaming agent
thermoplastic 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.)
Pending
Application number
JP57202589A
Other languages
Japanese (ja)
Inventor
Seiji Saka
坂 聖二
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.)
Mitsuboshi Belting Ltd
Original Assignee
Mitsuboshi Belting 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 Mitsuboshi Belting Ltd filed Critical Mitsuboshi Belting Ltd
Priority to JP57202589A priority Critical patent/JPS5991039A/en
Publication of JPS5991039A publication Critical patent/JPS5991039A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/16Auxiliary treatment of granules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/002Methods

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To make cells uniform and fine, to make the diffusion of a gas in a molded item good, and to make the shock resistance good, by impregnating a thermoplastic resin with a halogenated hydrocarbon containing at least one fluorine followed as a foaming agent by injection molding. CONSTITUTION:The foaming agent should have a boiling point in the range of -90-50 deg.C under normal pressures, and examples of the foaming agents are CHClF2, CCl2F2, CClF2-CClF2, CCl3F, etc. First, pellets of a thermoplastic resin are charged into a high pressure tank, and then a foaming agent is charged into said tank at room temperature under 1-20kg/cm<2> thereby impregnating the resin therewith. In this case, if the amount of the impregnation is 0.5-10wt%, the gasifying rate at room temperature under normal pressures is low, therefore an enough amount of a gas is generated during the molding to attain the aimed foaming rate, and the gas in the molded item can be released within a short period of time, so that the degassing period can be shortened and the adverse effect of the gas in the case of painting can be obviated.

Description

【発明の詳細な説明】 氷光明は、射出成形によって侵ら−する主とし°Cスキ
ン1Δと発泡1ωのザンドイッチ構造となるストラクチ
ャルフオームの如き熱i、jJ i性MW脂発r(iA
 Ij2形品の製it”i ’J−j法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION Hyokomei is a structural form that has a Zandwich structure of mainly °C skin 1Δ and foaming 1ω that is eroded by injection molding.
This relates to the method for manufacturing Ij2 type products.

従来、ポリアミド、ポリエステル、改質ポリフェニレン
オキサイド、ABS、ポリスチレンの如さ持に高1蝕点
重合体を発泡射出成形する場合、従来JIjitl剤と
してアゾ系、ニトロソ系、ヒドラジン糸等の化学発泡剤
が使用され、なかでもアゾ・ジ・カーボンアミドは最も
一般的に良く用いられている。しかし、これ等の発1゛
d7和は優れた発泡性能を示す反面、発泡剤残渣がボス
Conventionally, when performing foam injection molding of high corrosion point polymers such as polyamide, polyester, modified polyphenylene oxide, ABS, and polystyrene, chemical blowing agents such as azo, nitroso, and hydrazine threads have been used as JIJITL agents. Among them, azo dicarbonamide is the most commonly used. However, while these foaming 1゛d7 sums exhibit excellent foaming performance, the foaming agent residue is the problem.

リブ、穴等につまり数ショットごとに取り除く作業を必
娶とし、はつ残渣によるモ′−ルドの錆や腐蝕を発生さ
せる等大きな欠点を有している。
This method has major drawbacks such as the fact that the mold gets clogged with ribs, holes, etc. and must be removed every few shots, and the mold gets rusted and corroded by the mold residue.

さらに、これ等の泪泡刑卒がご用した成形物は該成形内
のカス拡散速度が伽<、成形後すぐに塗装すると成形品
内部のガスが産膜を持ち上げて無数の小さなムくれを発
生せしめる基本的な欠点があり、そのため7〜3日11
1jのガス抜は助+1FJ成形品をストックしなければ
、fiらない難点を有していた。しかも、分解物中にア
ンモニアを含むため作業環境は好ましくない。
Furthermore, the molded products used by these tearful executors have a low rate of scum diffusion within the molding, and if painted immediately after molding, the gas inside the molded product will lift the film and cause countless small swellings. There is a basic drawback that causes it to occur, so 7 to 3 days 11
The problem with degassing the 1j was that it could not be completed unless the Suke+1FJ molded product was stocked. Moreover, since the decomposition products contain ammonia, the working environment is not favorable.

一方、物理発泡剤として使用されている窒素ガスについ
ては、スクリューで?−脂を可塑化している最中に窒素
ガスを圧入し分散させる方法が採用されているが、窒素
ガスの分散が不充分で成形品内部に大きなボイドが発生
しやすいといった大きな欠点をもっている。また、この
方法で得られた成形品を塗装する場合でも化学発泡剤を
用いたのと同様に3〜3日IKJのガス抜き時間が必要
である。
On the other hand, what about nitrogen gas, which is used as a physical blowing agent, with a screw? - A method has been adopted in which nitrogen gas is forced in and dispersed during the plasticization of the fat, but this method has a major drawback in that the nitrogen gas is not sufficiently dispersed and large voids are likely to occur inside the molded product. Further, even when painting a molded article obtained by this method, it is necessary to degas the IKJ for 3 to 3 days, as in the case of using a chemical foaming agent.

史に、L記化学発泡法および窒素ガス物理発泡法でju
らIた発泡成形品はその表面に発生した荒れ(スワール
)によって1lii1衝撃性に欠けると共に塗装品質を
低下させている。
Historically, chemical foaming method and nitrogen gas physical foaming method have been used to
Due to the roughness (swirl) generated on the surface of the foamed molded product, it lacks impact resistance and also reduces the quality of the coating.

かくして本発明は上述の如き問題に着目し、その欠点を
排除し高融点重合体の発泡成形といえどもモールドの錆
や腐蝕の発生の懸念がなく、かつ成ノ1ソ俣の〉6泡成
形品のガス抜き時間を短かくしたl1li−1衝撃性を
−fnする発泡成形品を製造する方法を提供することを
目的とするものであり、その侠旨とするところは、発泡
剤として少なくとも7個以上のフッ素を言むハロゲン化
炭化水素を予め所定の圧力下において熱可塑性樹脂に含
浸させてこれを射出成形するにあり、熱用世性f+’、
J脂中に対して上記発泡剤の溶解度が従来の発泡剤に比
べて大きいため予め熱可塑性樹脂に含浸させてこれを発
泡成形するために均一な発泡成形品が得られ、また本発
明で使用する発泡剤は゛線圧時における沸点が高いため
に室温時における発泡剤のガス化速度をおさえて射出成
形時に発泡剤のガス発生量を多くすることができ、更に
は成形体内部に伴圧するガスは魚時間に成形体外部−\
放出できる特性を有しており、これによって5d泡成形
品のガス抜き時Illを短かくし、かつ塗装の際のガス
被害を少なくしている。
Thus, the present invention has focused on the above-mentioned problems, eliminates the drawbacks, eliminates the concern of mold rust and corrosion even when foam molding is performed using a high melting point polymer, and achieves the following foam molding in a timely manner. The purpose of this invention is to provide a method for producing a foam molded product that shortens the degassing time of the product and has -fn impact resistance. The thermoplastic resin is impregnated with a halogenated hydrocarbon containing fluorine or more under a predetermined pressure and then injection molded.
The solubility of the above-mentioned blowing agent in J resin is higher than that of conventional blowing agents, so a uniform foamed molded product can be obtained because it is impregnated with a thermoplastic resin in advance and then foam-molded, and also used in the present invention. The blowing agent has a high boiling point under linear pressure, so it is possible to suppress the gasification rate of the blowing agent at room temperature and increase the amount of gas generated by the blowing agent during injection molding. is the outside of the molded body during the fish time.
It has the property of being able to be released, thereby shortening Ill during degassing of 5D foam molded products and reducing gas damage during painting.

ここで、本発明で使用する発泡剤は少なくとも7個以北
のフッ素原子を含むハロゲン1ヒ炭化圧 水素であって常在時の沸点−タO℃〜!o℃の範囲にあ
り、具体的ニハCHCe Fx 、 CCetFm。
Here, the blowing agent used in the present invention is a halogen arsenic hydrocarbon containing at least 7 or more fluorine atoms, and has a boiling point of −0° C. when present. ℃ range, specifically Niha-CHCe Fx, CCetFm.

CCe F!−CCe F!、 アルイi、tc ce
s F 等テする。
CCe F! -CCe F! , Aluii, tc ce
s F etc.

かかる殆削剤は熱可塑性樹脂に含浸されるが、まず熱可
塑性樹脂ペレットを高圧用タンク内に入れ、その後発泡
剤を/〜、!0シ/ cd 、 g温の条件Fのタンタ
内に投入して発泡剤を熱可塑性樹脂ペレットに含浸(溶
解)させる。この傷合、発泡剤の含浸度はO,S〜70
瓜以%であり、この範囲の含浸量であると成形時のガス
発生量が重量となって最7雌な発泡倍率をもつ成形品が
得られる。
Such a cutting agent is impregnated with a thermoplastic resin, but first the thermoplastic resin pellets are placed in a high-pressure tank, and then a blowing agent is added. The foaming agent is impregnated (dissolved) into the thermoplastic resin pellet by putting it into a tantalum under condition F at a temperature of 0 c/d and g. The degree of impregnation of the foaming agent in this wound is O, S ~ 70
If the amount of impregnation is within this range, the amount of gas generated during molding becomes the weight, and a molded product with an expansion ratio of up to 7% can be obtained.

なお1丁f+L!第1表および第2表は夫々改質ポリフ
ェニレンオキサイドに対するCHCeFg(フレオン2
2)とN2の最大溶解+Aに関する結果であるが、本発
明で使用する@泡剤は窒素ガスに比べて溶解性において
はるかに侵れていることを示しており、これによって予
め熱可塑性樹脂に発泡剤を含浸させることが可能となり
、また本発明で用いる)6泡剤は611点が商いために
室温、音圧下においてガス化速度が小さく、そのため発
削剤の含浸した熱可1y1性樹脂は室温において発泡剤
のガス化が起りにくくなって成形時に十分なガスを発生
させろことができて目的とする発泡倍率をもつ成形品を
得ることができる。
In addition, 1 f+L! Tables 1 and 2 show CHCeFg (Freon 2) for modified polyphenylene oxide, respectively.
2) and the results regarding the maximum dissolution +A of N2, it is shown that the @ foaming agent used in the present invention has a much higher solubility than nitrogen gas, and this results in Since the foaming agent used in the present invention has a 611 point value, the gasification rate is low at room temperature and under acoustic pressure. Gasification of the blowing agent is less likely to occur at room temperature, and sufficient gas can be generated during molding, making it possible to obtain a molded article with the desired expansion ratio.

以下空白 第 / 表 樹脂に含浸するフレオン2.2の最大嵐(型部%)第、
2表 位(脂に含浸するN2の最大域(重量%)本発明で使用
する熱り塑性樹脂としてはポリアミド、ポリエステル、
改質ポリフェニレンオキサイド、ABS、ポリスチレン
の如き200〜300’QCI’)^蚤融点爪合体が使
用され、また成形γm1度も査1・j(脂に応じて選定
さね、ろが、これら)樹脂では通常、200 ’C以上
であり、このため熱可塑性;+!脂中に含浸した元71
剤のガス化速度は大きくlCってガス発生域が急激に羽
加し、適度な発泡倍率をもつ成形体が得られる。
Blank number below / Maximum storm of Freon 2.2 impregnated into surface resin (mold part %) number,
2 surface (maximum range of N2 impregnated into fat (wt%)) The thermoplastic resins used in the present invention include polyamide, polyester,
Modified polyphenylene oxide, ABS, polystyrene, etc. (200-300'QCI') are used, and molding γm 1 degree is also examined (1, 1, 1, 2, 3, etc.) resins (select according to the fat, filter, etc.) It is usually above 200'C and therefore thermoplastic;+! Original 71 impregnated in fat
The gasification rate of the agent is large, and the gas generation region rapidly increases, resulting in a molded product with an appropriate expansion ratio.

また、射出成形については通常の射出成形機が使用さ第
1、射出成形機は種々の成形機でよいが、主にストラク
チャルフオーム用の専用成形機が使用される。
For injection molding, a normal injection molding machine is used, but various types of injection molding machines may be used, but a special molding machine for structural foam is mainly used.

以ド引続き、実施例を挙げて更に具体的に説明する。Hereinafter, the present invention will be described in more detail with reference to Examples.

(実施例1) 比fJ7 /、 /の改質ポリフェニレンオキサイドを
ランク1ノ」に入れた後、3T’y/cm、20°Cの
条件トにおいて故状のフレオン22 (CHceF* 
分子il!g乙、沸点−ti / ”C)を投入して、
フレオン22を2形含浸させた改質ポリフェニレンオキ
サイドを得、これを低圧のSF専用マシン(EX7Co
ee−0社’S ’l OOトン)を用イシリンダー、
マニホールドとも一乙O′Cで成形した。得られた成形
体は均一微細気泡を合し、発泡倍率は/1.2倍であっ
たUまた。100シヨツト成形後もモールドに錆の発明
は認められず、成形2時間後塗装しても塗膜にba常は
認められなかった。
(Example 1) After adding a modified polyphenylene oxide with a ratio of fJ7 /, / to rank 1, Freon 22 (CHceF*
Molecule il! gB, boiling point -ti/"C) is added,
Modified polyphenylene oxide impregnated with type 2 Freon 22 was obtained, and this was processed using a low-pressure SF machine (EX7Co).
ee-0 company'S 'l OOton) is used for cylinder,
Both manifolds were molded using Ichitsu O'C. The obtained molded product had uniform fine cells, and the expansion ratio was 1.2 times. Even after 100 shots were molded, no rust was observed on the mold, and even after painting 2 hours after molding, no ba was observed on the coating film.

なお、落球衝撃性を測定したが、これは直径/インチで
重さ1.まりの球を厚さ6藺の成形体の七に落下して成
形体に亀裂が生じた時の球のFJt”Mさと球の重量の
債によって求められるもので、木実雄側では1Iosν
、CMであった。
In addition, the falling ball impact resistance was measured, and this was measured in terms of diameter/inch and weight of 1. It is determined by the equation of FJt"M of the ball and the weight of the ball when a crack occurs in the molded object when it falls into the middle of a molded object with a thickness of 6.
, it was a commercial.

(実施例2) 実施例1と同様の方法によってフレオン/2(Ccgz
 F、分子、1/ 、20.9 、7>’li点−、z
y、、r’c)を、2.g重速%含浸させた比重/、/
の改質ポリフェニレンオキサイドを実施例1と同様の成
形条件で成形したU得られた成形体は均一微細気泡を1
」シ、発泡倍率は/・2ひあった。また、10Oシコツ
I−所もモールドに錆の発生は認められず、成形Ω時間
後りi装しても塗11’4に異常はa&ぬられべCか−
)だ。
(Example 2) Freon/2 (Ccgz
F, molecule, 1/, 20.9, 7>'li point -, z
y,, r'c), 2. g weight rate % impregnated specific gravity /, /
The modified polyphenylene oxide was molded under the same molding conditions as in Example 1. The molded product obtained contained 1 uniform fine cell.
The foaming ratio was 2. In addition, no rust was observed on the mold at the 100 point I point, and even after the molding Ω hours had passed, there was no abnormality in the coating 11'4.
)is.

なお、落ト11月1四1生はグ03t・(7)でΔ)−
〕た。
In addition, for the fallen November 141 student, Δ)- is gu03t・(7).
〕Ta.

(実実名イ列3 ) 1、Js EA y、 /の酸1−1ポリフェニレンオ
キサイドをタンク内に入れた後、3 Ky / ctR
コO′Cの条件[ニオイ’Cを原状(7)’7L/オン
//II(CCeF*’−CC1!F1分子17j /
 70.り、811点3.ざ’O)を投入して、フレオ
ン//’Iを1%含浸させ、こtlを実施例1と同様の
成形条件で成形した。得られた成形体は実施例1.2と
同じ結果が得られた。
(Real name column 3) 1. After putting the acid 1-1 polyphenylene oxide of Js EA y, / into the tank, 3 Ky / ctR
Conditions for O'C [Odor'C in its original state (7)'7L/on//II (CCeF*'-CC1!F1 molecule 17j/
70. 811 points 3. The material was impregnated with 1% Freon//'I, and molded under the same molding conditions as in Example 1. The obtained molded product had the same results as Example 1.2.

(比較例1) 比重/、/の改質ポリフェニレンオキサイド100車量
部にアゾシカ−ボンアミドO0S瓜颯部をタンブラ−に
て混合し実施例1と同一条件で成形した。イ髪tらtま
た成形品は均一微細気泡をf−T L/ 発泡倍率は7
.2倍であったが、100シヨツト成形後、モールドに
錆が発生し、またモールドおよび成形物に残液が認めら
れた。成形後、2時間経過後塗装すると塗膜に無数のふ
くれが認められた。なお、落球衝41(性は、2.2.
ff〜・鋼であった。
(Comparative Example 1) 100 parts by volume of modified polyphenylene oxide with a specific gravity of /, / were mixed with azocabonamide O0S in a tumbler, and molded under the same conditions as in Example 1. In addition, the molded product has uniform fine bubbles.The foaming ratio is 7.
.. However, after 100 shots were molded, rust occurred on the mold, and residual liquid was observed on the mold and molded product. When painted 2 hours after molding, numerous blisters were observed in the coating film. In addition, the falling ball impact 41 (gender is 2.2.
ff~・It was steel.

(比較例2) 比重/、/の改質ポリフェニレンオキサイド700重量
部に窒素ガスo、g爪量の割合で該樹脂のtBJ塑化中
に圧入し、その池の成形条件は実施例1と同様である。
(Comparative Example 2) 700 parts by weight of modified polyphenylene oxide with a specific gravity of It is.

得られた成形品は発泡倍率が7.2倍であったが、内部
に大きなボイドを有する11所があった。また、100
シヨツト成形後もモールドに錆の発生は認められなかっ
たが、成形2時間後塗装すると塗膜に無数の小さなふく
れが発生した。なお、落球衝撃性は、22j9・画と小
さく、成形品は耐鉤撃性に欠けるものであった。
The obtained molded product had an expansion ratio of 7.2 times, but there were 11 large voids inside. Also, 100
No rust was observed on the mold after shot molding, but when it was painted 2 hours after molding, numerous small blisters appeared on the paint film. The ball impact resistance was as low as 22j9, and the molded product lacked hook resistance.

以tのように本発明方法によると、少なくとも7個以上
のフッ素を含むハロゲン化炭化水素からなる発泡剤が熱
可塑性初詣に含浸しやすく。
As described below, according to the method of the present invention, a blowing agent made of a halogenated hydrocarbon containing at least seven fluorine atoms is easily impregnated into the thermoplastic hatsumode.

そして発泡剤のガス化速度が室温において小さくて成形
温度にJゴいて大きくなるため、均一微細気泡を何する
成形品ル得ることが出来、またト記発泡剤から生じたガ
スも成形体中の拡散が良好であるために発泡成形品のカ
ス抜き時間を短かくして塗装の際のガス仮吉もなくなり
、また金型腐蝕の問題も起らず、し7かも耐衝撃性の良
好な光重成形品が得られZ、ものである。
Since the gasification rate of the blowing agent is low at room temperature and increases as the molding temperature increases, it is possible to obtain a molded product with uniform micro-cells, and the gas generated from the blowing agent also Good diffusion reduces waste removal time from foamed molded products, eliminates gas leaks during painting, and eliminates mold corrosion problems.7 Moreover, light heavy molding has good impact resistance. The product is Z, and it is a thing.

Claims (1)

【特許請求の範囲】[Claims] 1、’56 KjJ剤として少なくとも/個以りのフッ
系を含むハロゲン化炭化水素を予め熱可塑性樹脂に含f
場させ、かくして得られた熱可塑性樹脂を発泡射出成形
することを特徴とする発泡成形品のび・a造方法。
1, '56 Preliminary addition of at least/more fluorine-containing halogenated hydrocarbons to the thermoplastic resin as a KjJ agent.
1. A method for stretching and forming a foam molded product, which is characterized in that the thermoplastic resin thus obtained is foamed and injection molded.
JP57202589A 1982-11-17 1982-11-17 Manufacture of foamed and molded item Pending JPS5991039A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57202589A JPS5991039A (en) 1982-11-17 1982-11-17 Manufacture of foamed and molded item

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57202589A JPS5991039A (en) 1982-11-17 1982-11-17 Manufacture of foamed and molded item

Publications (1)

Publication Number Publication Date
JPS5991039A true JPS5991039A (en) 1984-05-25

Family

ID=16459981

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57202589A Pending JPS5991039A (en) 1982-11-17 1982-11-17 Manufacture of foamed and molded item

Country Status (1)

Country Link
JP (1) JPS5991039A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5167366A (en) * 1974-12-10 1976-06-10 Asahi Chemical Ind HORIAMIDOHATSUHOTAINO SEIZOHOHO
JPS5927928A (en) * 1982-08-06 1984-02-14 Du Pont Mitsui Fluorochem Co Ltd Foaming composition of modified polyphenylene oxide and its production

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5167366A (en) * 1974-12-10 1976-06-10 Asahi Chemical Ind HORIAMIDOHATSUHOTAINO SEIZOHOHO
JPS5927928A (en) * 1982-08-06 1984-02-14 Du Pont Mitsui Fluorochem Co Ltd Foaming composition of modified polyphenylene oxide and its production

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