JPS59133233A - Production of pre-expanded particle of polypropylene resin - Google Patents

Production of pre-expanded particle of polypropylene resin

Info

Publication number
JPS59133233A
JPS59133233A JP774383A JP774383A JPS59133233A JP S59133233 A JPS59133233 A JP S59133233A JP 774383 A JP774383 A JP 774383A JP 774383 A JP774383 A JP 774383A JP S59133233 A JPS59133233 A JP S59133233A
Authority
JP
Japan
Prior art keywords
expanded
expansion ratio
particles
expanded particles
polypropylene 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
Application number
JP774383A
Other languages
Japanese (ja)
Other versions
JPH0355502B2 (en
Inventor
Hideki Kuwabara
英樹 桑原
Toru Yamaguchi
徹 山口
Yoshimi Sudo
好美 須藤
Shohei Yoshimura
吉村 正平
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 JP774383A priority Critical patent/JPS59133233A/en
Priority to US06/536,847 priority patent/US4504601A/en
Priority to EP83109827A priority patent/EP0108245B1/en
Priority to DE8383109827T priority patent/DE3375015D1/en
Publication of JPS59133233A publication Critical patent/JPS59133233A/en
Publication of JPH0355502B2 publication Critical patent/JPH0355502B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To obtain pre-expanded particles having a heightened expansion ratio and a large cell diameter and being capable of forming a foam of a good dimensional accuracy and strong nerve, by heating, with steam, pre-expanded PP resin particles having a specified relationship between the expansion ratio and the number of cells. CONSTITUTION:Pre-expanded particles having an expansion ratio which is higher than the initial expansion ratio are produced by expanding, by heating with steam, pre-expanded PP resin particles having a relationship: 2<E<1/2>Xn<1/245, wherein E is an expansion ratio and n is the number of cells per mm.<2>-cross-sectional area. According to this process, it is possible to produce easily pre-expanded PP resin particles which have a high content of closed cell even at a high expansion ratio of, say, about 50-150, and can be used in molding. It is possible to obtain a molding of a strong nerve and a good dimensional accuracy and good moldability in both cases of low and high expansion.

Description

【発明の詳細な説明】 本発明はポリプロピレン系樹脂予備発泡粒子の製造方法
に関し、さらに詳しくは成型性が良好なポリプロピレン
系樹脂予備発泡粒子の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing pre-expanded polypropylene resin particles, and more particularly to a method for producing pre-expanded polypropylene resin particles having good moldability.

従来より主に発泡ポリスチレン、発泡ポリエチレンが緩
衝材、包装材等各方面に用いられている。
Conventionally, foamed polystyrene and foamed polyethylene have been mainly used for various purposes such as cushioning materials and packaging materials.

これらの発泡体と共にポリプロピレン系樹脂の発泡成型
体が使用されてきており2本出願人はポリプロピレン系
樹脂のビーズ成型法に用いる予備発泡粒子を得る方法を
すでに出願している(%公昭56−1344号)。この
方法によれば2発泡が非常に困難とされていた。ポリプ
ロピレン系肩脂粒子から簡単に比較的高発泡の予備発泡
粒子を得ることができる画期的なものであるが、同時に
次の様な問題点を有しており、未だ改良の余地を残して
いるものである。すなわち。
Along with these foams, polypropylene resin foam moldings have been used, and the applicant has already filed an application for a method for obtaining pre-expanded particles used in a polypropylene resin bead molding method (Kokusho 56-1344). issue). According to this method, it was considered very difficult to form two foams. Although this is an epoch-making method that allows relatively highly foamed pre-expanded particles to be easily obtained from polypropylene shoulder fat particles, it also has the following problems, and there is still room for improvement. It is something that exists. Namely.

fl)  比較的高発泡のものが得られるとはいえ、2
5倍程度が限度であり、これ以上の倍率のものを得よう
としても独立気泡率の低下を招き成型に供し得ない。
fl) Although relatively high foaming can be obtained, 2
The limit is about 5 times, and even if you try to obtain a product with a magnification higher than this, the closed cell ratio will decrease and it will not be possible to use it for molding.

(2)  得られる予備発泡粒子の気泡が4に細となる
傾向があり、このような予備発泡粒子を用いて成型体を
得ようとしても寸法精度が良好で腰の強い発泡体は得難
い。
(2) The cells of the obtained pre-expanded particles tend to be as small as 4, and even if it is attempted to obtain a molded article using such pre-expanded particles, it is difficult to obtain a strong foam with good dimensional accuracy.

本発明は上記従来技術の問題点を克服することを目的と
したものである。すなわち本発明の目的の一つは、高発
泡1例えば50〜150倍程度の発泡倍率であっても独
立気泡率が高く成型に供し得るポリプロピレン系樹脂予
備発泡粒子を簡単に製造し得る方法を提供することであ
る。本発明の他の目的は、低発泡、高発泡のいずれであ
っても成型性が良好で、腰が強く2寸法精度の良好な成
型体を得ることができるポリプロピレン系樹脂予備発泡
粒子を容易に製造し得る方法を提供することである。
The present invention aims to overcome the problems of the prior art described above. That is, one of the objects of the present invention is to provide a method for easily producing pre-expanded polypropylene resin particles that have a high closed cell ratio and can be molded even when the expansion ratio is high, for example, 50 to 150 times. It is to be. Another object of the present invention is to easily produce pre-expanded polypropylene resin particles that have good moldability regardless of whether they are low-foamed or highly foamed, and are strong and can yield molded bodies with good two-dimensional accuracy. The object of the present invention is to provide a method for manufacturing the same.

本発明者らは上記目的を達成すべく鋭意研究した結果1
発泡倍率および気泡数が特定の関係を有するポリプロピ
レン系樹脂予備発泡粒子を蒸気にて加熱することにより
発泡倍率が向上され、かつ気泡径が大きく(気泡数が少
なく)なった予備発泡粒子が得られ、かかる予備発泡粒
子は成型性に優れ、これを用いて得られる発泡成型体は
2寸法精度が良好な腰が強いものであることを見出し。
As a result of intensive research by the present inventors in order to achieve the above object, 1
By heating pre-expanded polypropylene resin particles with a specific relationship between the expansion ratio and the number of cells with steam, the expansion ratio is improved and pre-expanded particles with a larger cell diameter (smaller number of cells) can be obtained. It was discovered that such pre-expanded particles have excellent moldability, and that the foamed molded product obtained using the same has good two-dimensional accuracy and is strong.

本発明を完成するに至った。The present invention has now been completed.

すなわち9本発明は発泡倍率をE、断面1m”当りの気
泡数をnとしたとき2次式:2<E”Xn””<45の
関係を満足するポリプロピレン系樹脂予備発泡粒子を蒸
気にて加熱して発泡させ。
In other words, in the present invention, pre-expanded polypropylene resin particles satisfying the relationship of the quadratic formula: 2<E" Heat and foam.

元の発泡倍率Eより大なる発泡倍率を有する予備発泡粒
子を得ることを特徴とするポリプロピレン系樹脂予備発
泡粒子の製造方法を要旨とするものである。
The gist of this invention is a method for producing pre-expanded polypropylene resin particles, which is characterized by obtaining pre-expanded particles having an expansion ratio greater than the original expansion ratio E.

本発明に用いられるポリプロピレン系樹脂としては2例
えばプロピレン単独重合体、エチレン−プロピレンラン
ダム共重合体、エチレンーグロビレンブロック共重合体
、これらの混合物等が挙げられるが、エチレン−プロピ
レンランダム共重合体が特に好ましい。
Examples of the polypropylene resin used in the present invention include propylene homopolymers, ethylene-propylene random copolymers, ethylene-globylene block copolymers, mixtures thereof, and ethylene-propylene random copolymers. is particularly preferred.

本発明において発泡に供されるポリプロピレン系樹脂予
備発泡粒子としては2発泡倍率をE、断面1闘2当りの
気泡数をnとしたとき1次式:2く1/3  1/2 
< 45を満足する予備発泡粒子でE      Xn ある。E1/3  1/2が2以下ではこれを加熱発×
 n 泡して得られる予備発泡粒子の気泡が粗大となり過ぎ、
良好な物性を有する発泡成型体が得られ難l/ a  
 s / xが45以上の場合(かかる場い。E   
Xn 合は発泡倍率Eが極端に高いか気泡数nが極端に多いか
いずkあ場合、もしくは両方の場合である。Yには、こ
のような予備発泡粒子を加熱して発泡させようとしても
収縮が生じ易く2発泡効率が極めて悪くなり、無理に発
泡させようとすれば独立気泡率の低下を招く、このよう
にして得られた予備発泡粒子を用いて2発泡成型を行な
ったとしても得られる発泡成型体は寸法精度に劣り、満
足な物性を有するものではない。
In the present invention, the polypropylene resin pre-expanded particles used for foaming are expressed by the linear formula: 2 x 1/3 1/2 where the expansion ratio is E and the number of bubbles per cross section is n.
E Xn is a pre-expanded particle that satisfies <45. If E1/3 1/2 is less than 2, heat it
n The bubbles of the pre-expanded particles obtained by foaming become too coarse,
It is difficult to obtain a foam molded product with good physical properties l/a
When s/x is 45 or more (in such cases, E
In the case of Xn, the expansion ratio E is extremely high, the number of bubbles n is extremely large, or both are the case. In Y, even if such pre-expanded particles are heated and foamed, they tend to shrink, resulting in extremely poor foaming efficiency, and if they are forced to foam, the closed cell ratio will decrease. Even if two-foam molding is performed using the pre-expanded particles obtained in this manner, the resulting foamed molded product has poor dimensional accuracy and does not have satisfactory physical properties.

本発明において、加熱発泡に供される出発原料としての
最初の予備発泡粒子は例えば以下の方法によって得るこ
とができる。すなわち、ポリプロピレン系樹脂粒子、揮
発性発泡剤および分散媒を密閉容器内に入れ、樹脂粒子
が軟化する温度以上の温度に加熱して揮発性発泡剤を樹
脂粒子に含有させ2次いで容器の一端を開放して樹脂粒
子と分散媒を同時に容器内よりも低圧の雰囲気に放出す
ることにより得ることができる。
In the present invention, the first pre-expanded particles as a starting material to be subjected to heat foaming can be obtained, for example, by the following method. That is, polypropylene resin particles, a volatile blowing agent, and a dispersion medium are placed in a closed container, and heated to a temperature higher than the temperature at which the resin particles soften to incorporate the volatile blowing agent into the resin particles. This can be obtained by opening the container and simultaneously releasing the resin particles and the dispersion medium into an atmosphere having a lower pressure than the inside of the container.

本発明において、予備発泡粒子に積極的に発泡能を付与
することは特に必要としない。しかし。
In the present invention, it is not particularly necessary to actively impart foaming ability to the pre-expanded particles. but.

元の予備発泡粒子に対し1.4倍以上に発泡させる場合
や元の発泡粒子が10倍以下の場合には一回の発泡操作
では高発泡粒子が得られないので発泡能を付与すること
が好ましい。
If the original pre-expanded particles are expanded to 1.4 times or more, or if the original expanded particles are 10 times or less, it is not possible to obtain highly expanded particles with a single foaming operation, so it is necessary to add foaming ability. preferable.

発泡能の付与は予備発泡粒子に無機ガス、揮発性発泡剤
、または無機ガスと揮発性発泡剤との混合ガスを含有さ
せることにより行々われ、所望する発泡倍率の程度によ
っても異なるが2通常1.5〜1o ky / d(G
)の内圧が付与される。無機ガスとしては1例えば、空
気、窒素、アルゴン、ヘリウム等が挙げられるが通常は
空気が用いられる。また揮発性発泡剤としては2例えば
プロパン、ブタン、ペンタン、ヘキサノ等で例示される
脂肪族炭化水素類、シクロブタン、シクロペンタン等で
例示される環式脂肪族炭化水素類、トリクロロフロロメ
タン、ジクロロシフ0ロメタン、ジクロロテトラフロロ
エタン、メチルクロライド、エチルクロライド、メチレ
ンクロ2イド等で例示されるハロゲン化炭化水素類等を
使用することができる。
The foaming ability is imparted to the pre-expanded particles by containing an inorganic gas, a volatile foaming agent, or a mixed gas of an inorganic gas and a volatile foaming agent. 1.5~1oky/d(G
) is applied. Examples of the inorganic gas include air, nitrogen, argon, helium, etc., but air is usually used. Examples of volatile blowing agents include aliphatic hydrocarbons such as propane, butane, pentane, and hexano; cycloaliphatic hydrocarbons such as cyclobutane and cyclopentane; trichlorofluoromethane; Halogenated hydrocarbons such as lomethane, dichlorotetrafluoroethane, methyl chloride, ethyl chloride, methylene chloride, etc. can be used.

本発明において、ポリプロピレン系樹脂予備発泡粒子は
蒸気により加熱される。この加熱方法は。
In the present invention, the polypropylene resin pre-expanded particles are heated with steam. This heating method.

例えば予備発泡粒子を容器内に入れ攪拌しながら蒸気を
直接容器内へ導入することにより行なわれる。上記蒸気
としては2例えば0.5〜3に&/d(G)の水蒸気が
通常用いられ、また加熱時間は通常2分以内、好ましく
は1分以内である。このように蒸気を使用することによ
り熱風の場合よりも短時間に加熱することができ、また
高発泡粒子を得ることができ、その結果生産性が向上す
る。
For example, this is carried out by placing the pre-expanded particles in a container and introducing steam directly into the container while stirring. As the above-mentioned steam, 2, for example, 0.5 to 3&/d (G) steam is usually used, and the heating time is usually within 2 minutes, preferably within 1 minute. By using steam in this manner, heating can be performed in a shorter time than in the case of hot air, and highly expanded particles can be obtained, resulting in improved productivity.

1/s      1/2 本発明においては2次式:2(E   Xnく45の関
係を有するポリプロピレン系樹脂粒子を蒸気にて加熱し
て発泡させるが、この操作は一回の操作に制限されず、
加熱発泡させた予備発泡粒子をさらに蒸気にて加熱せし
め2発泡させる操作を繰り返してもよい。このような操
作は加熱発泡に供すべきポリプロピレン系樹脂予備発泡
粒子が上式の関係を満足する限り何度繰り返してもよい
1/s 1/2 In the present invention, polypropylene resin particles having the relationship of the quadratic formula: 2(E ,
The operation of heating and foaming the pre-expanded particles with steam and foaming them twice may be repeated. Such operations may be repeated any number of times as long as the polypropylene resin pre-expanded particles to be subjected to heat foaming satisfy the above relationship.

本発明において1発泡倍率Eは真の発泡倍率を意味する
。真の発泡倍率は予備発泡粒子の密度を基材樹脂の樹脂
密度で除した値の逆数である。ここで、予備発泡粒子の
密度は例えば次の如く測定することができる。まずメス
シリンダー中に予め入れておいた一定量の水の中に重量
既知の所定量の予備発泡粒子を入れた後全体の容積を測
定する。
In the present invention, 1 expansion ratio E means the true expansion ratio. The true expansion ratio is the reciprocal of the density of the pre-expanded particles divided by the resin density of the base resin. Here, the density of the pre-expanded particles can be measured, for example, as follows. First, a predetermined amount of pre-expanded particles with a known weight is placed in a predetermined amount of water previously placed in a graduated cylinder, and the total volume is then measured.

次いで全体の容積から元の水の体積を減じて予備発泡粒
子の容積を求め9重量を容積で除すことにより求めるこ
とができる。
Next, the volume of the pre-expanded particles can be determined by subtracting the original volume of water from the total volume, and dividing the weight by the volume.

本発明により得られる予備発泡粒子は通常元の予備発泡
粒子の発泡倍率の115倍以上の発泡倍率2例えば3〜
100倍、好ましくは10〜60倍の発泡倍率を有し、
また01〜200個/ i+m2の気泡数を有する。
The pre-expanded particles obtained by the present invention usually have an expansion ratio of 115 times or more than that of the original pre-expanded particles.
It has a foaming ratio of 100 times, preferably 10 to 60 times,
It also has a bubble count of 01 to 200/i+m2.

本発明により得られるポリプロピレン系樹脂予備発泡粒
子は発泡成型体の製造に用いられる。まず上記予備発泡
粒子は常温常圧上所定時間熟成された後、要すれば窒素
、空気等の無機ガスまたは揮発性発泡剤との混合ガスを
用いて所定圧力にて所定時間熟成される。次いで予備発
泡粒子は2例えば型面に水蒸気等の加熱媒体が通過でき
る小孔を有する金型に充填し2例えば2〜s kg /
 1(G)の水蒸気により加熱発泡させることにより型
通りの発泡成型体を得ることができる。
The pre-expanded polypropylene resin particles obtained according to the present invention are used for producing foam molded articles. First, the pre-expanded particles are aged at room temperature and pressure for a predetermined time, and then, if necessary, aged at a predetermined pressure for a predetermined time using an inorganic gas such as nitrogen or air, or a mixed gas with a volatile blowing agent. Next, the pre-expanded particles are filled into a mold having, for example, small holes on the mold surface through which a heating medium such as water vapor can pass, and the pre-expanded particles are packed at a rate of, for example, 2 to 2 s kg/2.
By heating and foaming with water vapor of 1(G), a foam molded product according to the shape can be obtained.

上記のポリプロピレン系樹脂発泡成型体は1例えば包装
材、緩衝材、保温材、断熱材、建築資材。
The polypropylene resin foam molded product mentioned above can be used, for example, as a packaging material, a cushioning material, a heat insulating material, a heat insulating material, and a construction material.

車輛部材、浮揚材1食品容器等に用いることができる。It can be used for vehicle parts, flotation material 1 food containers, etc.

以上説明したように2本発明によれば、より一層高発泡
のポリプロピレン系樹脂予備発泡粒子を得ることができ
、この予備発泡粒子を用いて得られる発泡成型体は、成
型性が一良好で、腰が強く。
As explained above, according to the present invention, it is possible to obtain pre-expanded polypropylene resin particles with even higher foaming, and the foamed molded article obtained using the pre-expanded particles has good moldability, I have a strong back.

かつ寸法精度が良好である等の優れた性質を有するもの
である。
It also has excellent properties such as good dimensional accuracy.

以下、実施例および比較例を掲けて本発明をさらに詳細
に説明する。
Hereinafter, the present invention will be explained in more detail with reference to Examples and Comparative Examples.

ロビレンランダム共重合体(融点145℃)予備発泡粒
子を容器内に入れ攪拌しながら第1表に示す圧力を有す
る水蒸気により直接加熱した。得られた予備発泡粒子に
空気にてz、skg/−J(絶対圧)の内圧を付与した
。次いでこの予備発泡粒子を金型に充填し、  3.2
 kg / cd CG)の水蒸気により加熱発泡させ
て発泡成型体を得た。得られた発泡成型体の寸法精度と
融着性を測定した。結果を第1表に示す。
Pre-expanded particles of Robylene random copolymer (melting point 145° C.) were placed in a container and heated directly with steam having a pressure shown in Table 1 while stirring. An internal pressure of z, skg/-J (absolute pressure) was applied to the obtained pre-expanded particles using air. The pre-expanded particles are then filled into a mold, 3.2
kg/cd CG) was heated and foamed with water vapor to obtain a foamed molded product. The dimensional accuracy and fusion properties of the obtained foam molded product were measured. The results are shown in Table 1.

※1−寸法精度は発泡成型体の収縮率により下記の如く
判定した。
*1 - Dimensional accuracy was determined as follows based on the shrinkage rate of the foam molded product.

1〜2%未満    0 2〜4%未満    Δ 4%以上    × ※2−融着性は長さ150zm、幅50闘、厚さ10闘
の試験片をテン/ロンにて500 鰭/ l1lI++
の速度で引張って破断させ、その断面の形状により下記
の如く判定した。
Less than 1 to 2% 0 Less than 2 to 4% Δ 4% or more
The specimen was pulled at a speed of 100 mL to break, and the shape of the cross section was evaluated as follows.

材質破壊      ○ 材質破壊と粒子間切断混合   △ 粒子間切断      X 手続補正書(自発) 昭和58年4月28e 特許庁長官 若杉和夫 殿 )Y” で− 1、事件の表示 昭和58年特許願第 7743 号 3、 補正をする者 事件との関係 特許出願人 住 所 東京都千代田区内幸町2丁目1番1号氏 名(
名称) 日本スチレンペー/く−株式会社代表者 長 
 野  和  吉 4、代理人〒101 5、 補正命令の日付    自 発 補 正8、補正
の内容  別 紙 の 通 リ。
Material destruction ○ Material destruction and interparticle cutting mixture △ Interparticle cutting No. 3. Relationship with the case of the person making the amendment Patent applicant address: 2-1-1 Uchisaiwai-cho, Chiyoda-ku, Tokyo Name (
Name) Japan Styrene Paper Co., Ltd. Representative Director
Kazuyoshi No 4, attorney 101-5, date of amendment order voluntary amendment 8, contents of amendment attached.

(1) F!A細書第6頁第7行の「騨/eJ(G)J
を[騨/d・abJと補正する。
(1) F! Book A, page 6, line 7, ``騨/eJ(G)J
is corrected as [騨/d・abJ.

(2>同第7頁第3行〜4行の「通常2分以内、好まし
くけ1分以内である。」を「通常1分以内、好ましくは
30秒以内である。」と補正する。
(2>"Usually within 2 minutes, preferably within 1 minute." in lines 3 and 4 of page 7 of the same page is corrected to "Usually within 1 minute, preferably within 30 seconds."

(3)同第11頁第1表中、処理前の予備発泡粒子の内
圧の項において、実施例1のaの値[2,2jをl” 
2.5 Jと補正し、実施例1のCの値「1.2Jを「
1.s Jと補正する。
(3) In Table 1 on page 11, in the section of internal pressure of pre-expanded particles before treatment, the value of a of Example 1 [2, 2j is l''
2.5 J, and the value of C in Example 1 is "1.2 J".
1. Correct it as s J.

(4)同表中蒸気圧力の項の単位「(K2/c11・q
)」をr(KP/eJ”aす」と補正する。
(4) The unit for steam pressure in the same table is “(K2/c11・q
)” is corrected as r(KP/eJ”asu”).

以   上that's all

Claims (1)

【特許請求の範囲】[Claims] 発泡倍率をE、断面1冨が当りの気泡数をnとしたとき
1次式: 2(E”” X n”” <45の関係を有
するポリプロピレン系樹脂予備発泡粒子を蒸気にて加熱
して発泡させ元の発泡倍率Eよシ大なる発泡倍率を有す
る予備発泡粒子を得ることを特徴とするポリプロピレン
系樹脂予備発泡粒子の製造方法。
When the expansion ratio is E and the number of cells per cross-section is n, the polypropylene resin pre-expanded particles having the relationship of: 2(E"" X n""<45) are heated with steam. A method for producing pre-expanded polypropylene resin particles, which comprises foaming the particles to obtain pre-expanded particles having a larger expansion ratio than the original expansion ratio E.
JP774383A 1982-10-01 1983-01-20 Production of pre-expanded particle of polypropylene resin Granted JPS59133233A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP774383A JPS59133233A (en) 1983-01-20 1983-01-20 Production of pre-expanded particle of polypropylene resin
US06/536,847 US4504601A (en) 1982-10-01 1983-09-29 Process for producing pre-foamed particles of polypropylene resin
EP83109827A EP0108245B1 (en) 1982-10-01 1983-09-30 Process for producing pre-foamed particles of polypropylene resin
DE8383109827T DE3375015D1 (en) 1982-10-01 1983-09-30 Process for producing pre-foamed particles of polypropylene resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP774383A JPS59133233A (en) 1983-01-20 1983-01-20 Production of pre-expanded particle of polypropylene resin

Publications (2)

Publication Number Publication Date
JPS59133233A true JPS59133233A (en) 1984-07-31
JPH0355502B2 JPH0355502B2 (en) 1991-08-23

Family

ID=11674177

Family Applications (1)

Application Number Title Priority Date Filing Date
JP774383A Granted JPS59133233A (en) 1982-10-01 1983-01-20 Production of pre-expanded particle of polypropylene resin

Country Status (1)

Country Link
JP (1) JPS59133233A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62115042A (en) * 1985-11-14 1987-05-26 Kanegafuchi Chem Ind Co Ltd Pre-expanded polyolefin resin particle and production thereof
JP2006022138A (en) * 2004-07-06 2006-01-26 Kaneka Corp Preliminary expanded polypropylene-based resin particle

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5431475A (en) * 1977-08-15 1979-03-08 Asahi Chem Ind Co Ltd Manufacture of both granular foam of crosslinked polyolefinic resin and formed product

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5431475A (en) * 1977-08-15 1979-03-08 Asahi Chem Ind Co Ltd Manufacture of both granular foam of crosslinked polyolefinic resin and formed product

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62115042A (en) * 1985-11-14 1987-05-26 Kanegafuchi Chem Ind Co Ltd Pre-expanded polyolefin resin particle and production thereof
JPH0554855B2 (en) * 1985-11-14 1993-08-13 Kanegafuchi Chemical Ind
JP2006022138A (en) * 2004-07-06 2006-01-26 Kaneka Corp Preliminary expanded polypropylene-based resin particle

Also Published As

Publication number Publication date
JPH0355502B2 (en) 1991-08-23

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