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JPH0355502B2 - - Google Patents
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JPH0355502B2 - - Google Patents

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Publication number
JPH0355502B2
JPH0355502B2 JP58007743A JP774383A JPH0355502B2 JP H0355502 B2 JPH0355502 B2 JP H0355502B2 JP 58007743 A JP58007743 A JP 58007743A JP 774383 A JP774383 A JP 774383A JP H0355502 B2 JPH0355502 B2 JP H0355502B2
Authority
JP
Japan
Prior art keywords
particles
expanded particles
expanded
polypropylene resin
expansion ratio
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
JP58007743A
Other languages
Japanese (ja)
Other versions
JPS59133233A (en
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 filed Critical
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

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Description

【発明の詳細な説明】[Detailed description of the invention]

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。 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。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、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(特
公昭56−1344号)。この方法によれば、発泡が非
常に困難とされていた、ポリプロピレン系樹脂粒
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、 (1) 比較的高発泡のものが得られるとはいえ、25
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。 (2) 得られる予備発泡粒子の気泡が微細となる傾
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。 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、例えば50〜150倍程度の発泡
倍率であつ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つても成型
性が良好で、腰が強く、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。 本発明者らは上記目的を達成すべく鋭意研究し
た結果、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)なつた予備発
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、寸法
精度が良好な腰が強いものであることを見出し、
本発明を完成するに至つた。 すなわち、本発明は発泡倍率をE、断面1mm2
りの気泡数をnとしたとき、次式:2<E1/3×
n1/2<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、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。 本発明に用いられるポリプロピレン系樹脂とし
ては、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−プロピ
レンブロツク共重合体、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。 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、発泡倍率をE、断
面1mm2当りの気泡数をnとしたとき、次式:2<
E1/3×n1/2<45を満足する予備発泡粒子である。
E1/3×n1/2が2以下ではこれを加熱発泡して得ら
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い。E1/3×
n1/2が45以上の場合(かかる場合は発泡倍率Eが
極端に高いか気泡数nが極端に多いかいずれかの
場合、もしくは両方の場合である。)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、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、発泡成型を行なつたとしても得られ
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。 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
によつ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、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。 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、
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。 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なわれ、所望す
る発泡倍率の程度によつても異なるが、、通常1.5
〜10Kg/cm2・abの内圧が付与される。無機ガス
としては、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、例えばプロパン、ブ
タン、ペンタン、ヘキサン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、ジクロロジフロロメタン、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、メチレンクロラ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。 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、例えば予備発泡粒子を容器内に入れ撹拌しな
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、例えば0.5〜3Kg/
cm2(G)の水蒸気が通常用いられ、また加熱時間は通
常1分以内、好ましくは30秒以内である。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。 本発明においては、次式:2<E1/3×n1/2<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、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。 本発明において、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。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、重量を容積で除すこ
とにより求めることができる。 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1.15倍以上の発泡倍
率、例えば3〜100倍、好ましくは10〜60倍の発
泡倍率を有し、また0.1〜200個/mm2の気泡数を有
する。 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下所定時間熟成さ
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、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、例えば2〜5Kg/cm2(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。 上記のポリプロピレン系樹脂発泡成型体は、例
えば包装材、緩衝材、保温材、断熱材、建築資
材、車輌部材、浮揚材、食品容器等に用いること
ができる。 以上説明したように、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、成型性が良好で、腰が強く、
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。 以下、実施例および比較例を掲げて本発明をさ
らに詳細に説明する。 実施例1〜16および比較例1〜15 常法により得られた第1表の1、第1表の2に
示す内圧を有するエチレン−プロピレンランダム
共重合体(融点145℃)予備発泡粒子を容器内に
入れ撹拌しながら第1表の1、第1表の2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2.5Kg/cm2(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、3.2Kg/cm2(G)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表の
1、2に示す。尚、これら実施例、比較例におい
て用いた予備発泡粒子のうち、処理前の予備発泡
粒子で発泡倍率が25倍を超える予備発泡粒子は実
施例のものは本発明方法に準じて2段発泡を行つ
て製造したものを用いた。これら得られたデータ
を、横軸をlogE、縦軸をlognとしてプロツトし
た(実施例は〇、比較例は●で示す。)結果を第
1図に示す。第1図中において直線1は、 logn=−2/3logE+2log45を、 また直線2は、 logn=−2/3logE+2log2を示し、直線1は 式:E1/3×n1/2=45に相当し、直線2は 式:E1/3×n1/2=2に相当する。
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. Conventionally, foamed polystyrene and foamed polyethylene have been mainly used for various purposes such as cushioning materials and packaging materials. 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 for use in a polypropylene resin bead molding method (Japanese Patent Publication No. 56-1344). issue). This method is revolutionary in that it is possible to easily obtain relatively highly foamed pre-expanded particles from polypropylene resin particles, which have been considered extremely difficult to foam. This method has some problems and still leaves room for improvement. In other words, (1) Although relatively high foaming can be obtained, 25
The limit is about twice as much, 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) The cells in the obtained pre-expanded particles tend to be fine, and even if a molded article is attempted to be obtained using such pre-expanded particles, it is difficult to obtain a strong foam with good dimensional accuracy. 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 at a high expansion ratio, for example, an expansion ratio of about 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, are strong, and can produce molded bodies with good dimensional accuracy, regardless of whether they are low-foamed or highly foamed. The object of the present invention is to provide a method for manufacturing the same. As a result of intensive research aimed at achieving the above object, the present inventors have found that by heating pre-expanded polypropylene resin particles with steam, which have a specific relationship between the expansion ratio and the number of cells, the expansion ratio can be improved, and the cell diameter can be improved. Pre-foamed particles with large (small number of bubbles) can be obtained, such pre-foamed particles have excellent moldability, and the foam molded product obtained using the same has good dimensional accuracy and is strong. Headline,
The present invention has now been completed. That is, in the present invention, when the expansion ratio is E and the number of bubbles per 1 mm 2 of cross section is n, the following formula: 2<E 1/3 ×
A polypropylene resin characterized in that pre-expanded polypropylene resin particles satisfying the relationship n 1/2 <45 are heated with steam and foamed to obtain pre-expanded particles having a larger expansion ratio than the original expansion ratio E. The gist of this paper is a method for producing pre-expanded resin particles. Examples of the polypropylene resin used in the present invention include propylene homopolymer, ethylene-
Examples include propylene random copolymers, ethylene-propylene block copolymers, mixtures thereof, and ethylene-propylene random copolymers are particularly preferred. The pre-expanded polypropylene resin particles used for foaming in the present invention are expressed by the following formula, where E is the expansion ratio and n is the number of cells per 1 mm 2 of cross section.
These are pre-expanded particles that satisfy E 1/3 ×n 1/2 <45.
If E 1/3 ×n 1/2 is less than 2, the bubbles in the pre-expanded particles obtained by heating and foaming will become too coarse, making it difficult to obtain a foamed molded product with good physical properties. E 1/3 ×
When n 1/2 is 45 or more (in such a case, either the expansion ratio E is extremely high or the number of cells n is extremely large, or both cases), such pre-foaming is necessary. Even if you try to foam the particles by heating them, they tend to shrink, resulting in extremely low foaming efficiency, and if you try to foam them forcibly, it will lead to a decrease in the closed cell ratio. Even if foam molding is carried out using this method, the resulting foam molded product has poor dimensional accuracy and does not have satisfactory physical properties. 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, heated to a temperature higher than the temperature at which the resin particles soften to incorporate the volatile blowing agent into the resin particles, and then one end of the container is closed. 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. In the present invention, it is not particularly necessary to actively impart foaming ability to the pre-expanded particles. but,
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, highly expanded particles cannot be obtained with a single foaming operation, so it is preferable to impart foaming ability. The foaming ability is imparted by allowing the pre-expanded particles to contain an inorganic gas, a volatile foaming agent, or a mixed gas of an inorganic gas and a volatile foaming agent, and varies depending on the desired expansion ratio. , usually 1.5
An internal pressure of ~10Kg/cm 2 ·ab 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 hexane, cycloaliphatic hydrocarbons such as cyclobutane and cyclopentane, trichlorofluoromethane, and dichlorodichloromethane. Halogenated hydrocarbons such as fluoromethane, dichlorotetrafluoroethane, methyl chloride, ethyl chloride, methylene chloride, etc. can be used. In the present invention, the polypropylene resin pre-expanded particles are heated with steam. This heating method is carried out, for example, by placing the pre-expanded particles in a container and introducing steam directly into the container while stirring. The above steam may be, for example, 0.5 to 3 kg/
cm 2 (G) of steam is usually used, and the heating time is usually within 1 minute, preferably within 30 seconds. 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. In the present invention, the following formula: 2<E 1/3 ×n 1/2 <45
Polypropylene resin particles having the following relationship are heated with steam and foamed, but this operation is not limited to one operation, and the pre-expanded particles that have been heated and foamed are further heated with steam to foam them. 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. In the present invention, the 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. The volume of the pre-expanded particles is then determined by subtracting the original water volume from the total volume, and can be determined by dividing the weight by the volume. The pre-expanded particles obtained by the present invention usually have an expansion ratio of 1.15 times or more than that of the original pre-expanded particles, for example, 3 to 100 times, preferably 10 to 60 times, and have an expansion ratio of 0.1 to 200 times. /mm 2 bubble count. 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 for a predetermined time at room temperature and pressure, and then aged for a predetermined time at a predetermined pressure using an inorganic gas such as nitrogen or air or a mixed gas with a volatile blowing agent, if necessary. Next, the pre-expanded particles are filled into a mold having small holes on the mold surface through which a heating medium such as water vapor can pass, and foamed according to the mold by heating and foaming with water vapor of, for example, 2 to 5 kg/cm 2 (G). A molded body can be obtained. The polypropylene resin foam molded product described above can be used, for example, in packaging materials, cushioning materials, heat insulating materials, heat insulating materials, construction materials, vehicle components, flotation materials, food containers, and the like. As explained above, according to the present invention, it is possible to obtain polypropylene resin pre-expanded particles with even higher foaming, and the foam molded product obtained using the pre-expanded particles has good moldability and stiffness. is strong,
It also has excellent properties such as good dimensional accuracy. Hereinafter, the present invention will be explained in more detail with reference to Examples and Comparative Examples. Examples 1 to 16 and Comparative Examples 1 to 15 Pre-expanded particles of ethylene-propylene random copolymer (melting point 145°C) having the internal pressure shown in 1 of Table 1 and 2 of Table 1 obtained by a conventional method were placed in a container. While stirring, the mixture was heated directly with steam having the pressures shown in Table 1, 1 and 2. 2.5Kg/cm 2 (absolute pressure) with air to the obtained pre-expanded particles
An internal pressure of . Next, the pre-expanded particles were filled into a mold and heated and foamed with 3.2 Kg/cm 2 (G) of steam 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 and 2. Among the pre-expanded particles used in these Examples and Comparative Examples, the pre-expanded particles with an expansion ratio exceeding 25 times before treatment were subjected to two-stage foaming according to the method of the present invention. I used the one that I had made there. The obtained data were plotted with the horizontal axis as logE and the vertical axis as logn (Examples are indicated by ○, comparative examples are indicated by ●). The results are shown in FIG. In Figure 1, straight line 1 shows logn = -2/3logE + 2log45, and straight line 2 shows logn = -2/3logE + 2log2, and straight line 1 corresponds to the formula: E 1/3 × n 1/2 = 45. , straight line 2 corresponds to the equation: E 1/3 ×n 1/2 = 2.

【表】【table】

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

第1図は実施例、比較例において得られた予備
発泡粒子の発泡倍率Eと気泡数nのデータに基
き、横軸をlogE、縦軸をlog nとしてプロツト
した図である。
FIG. 1 is a diagram plotted with the horizontal axis as logE and the vertical axis as log n, based on data on the expansion ratio E and the number of bubbles n of pre-expanded particles obtained in Examples and Comparative Examples.

Claims (1)

【特許請求の範囲】[Claims] 1 発泡倍率をE、断面1mm2当りの気泡数をnと
したとき、次式:2<E1/3×n1/2<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。
1 When the expansion ratio is E and the number of bubbles per 1 mm 2 of cross section is n, pre-expanded polypropylene resin particles having the following formula: 2 < E 1/3 × n 1/2 < 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 JPS59133233A (en) 1984-07-31
JPH0355502B2 true 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)

Families Citing this family (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
JP2006022138A (en) * 2004-07-06 2006-01-26 Kaneka Corp Preliminary expanded polypropylene-based resin particle
JP7525336B2 (en) * 2020-08-27 2024-07-30 株式会社カネカ Method for producing expanded polyolefin resin particles

Family Cites Families (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

Also Published As

Publication number Publication date
JPS59133233A (en) 1984-07-31

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