JPH1135731A - Preexpanded particle - Google Patents

Preexpanded particle

Info

Publication number
JPH1135731A
JPH1135731A JP9203869A JP20386997A JPH1135731A JP H1135731 A JPH1135731 A JP H1135731A JP 9203869 A JP9203869 A JP 9203869A JP 20386997 A JP20386997 A JP 20386997A JP H1135731 A JPH1135731 A JP H1135731A
Authority
JP
Japan
Prior art keywords
expanded particles
polystyrene resin
length
breadth
particles
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
JP9203869A
Other languages
Japanese (ja)
Inventor
Kunio Takahashi
邦雄 高橋
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.)
Achilles Corp
Original Assignee
Achilles 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 Achilles Corp filed Critical Achilles Corp
Priority to JP9203869A priority Critical patent/JPH1135731A/en
Publication of JPH1135731A publication Critical patent/JPH1135731A/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
    • B29B9/02Making granules by dividing preformed material
    • B29B9/06Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • 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
    • B29B9/12Making granules characterised by structure or composition

Abstract

PROBLEM TO BE SOLVED: To obtain preexpanded particles which give molded articles with less unevenness in coloration and hardly contg. voids among particles by preexpanding colored expandable polystyrene resin pellets in such a manner that the ratio of the length to the breadth of the resultant preexpanded particle is in a specified range. SOLUTION: A colored expandable polystyrene resin pellet having a length L and a breadth D is preexpanded by about 10-50 times in such a manner that the length L and the breadth D change into the length (l) and the breadth (d), respectively, of the resultant preexpanded particles and that the ratio of the length (l) to the breadth (d) satisfies the relation: 1<l/d<=4. The ratio of the length L to the breadth D is pref. 5-30. Pref., the length (l) satisfies the relation: W<=3 l (wherein W is the diameter of a filling port of a mold) in terms of easiness of mold filling.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、色むらがなく、粒
子間隙もない良好な成形品を得るための発泡性ポリスチ
レン系樹脂ペレットの予備発泡粒子に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to pre-expanded particles of expandable polystyrene resin pellets for obtaining a good molded article having no color unevenness and no particle gap.

【0002】[0002]

【従来の技術】従来より着色発泡性粒子の予備発泡粒子
を得るほう方法としては、発泡性ポリスチレン粒子の
表面に顔料や染料等の着色剤をヘンシェルミキサーやリ
ボンブレンダー等により均一にコーティング(まぶす)
する事により得られた着色発泡性粒子を予備発泡して予
備発泡粒子を得る。ポリスチレン粒子を水性媒体中で
均一に攪拌し、発泡剤を圧入すると共に、油溶性染料等
を投入して、粒子内に着色剤を含浸させて、着色発泡性
ポリスチレン粒子を得て、予備発泡して予備発泡粒子を
得る。着色発泡性ポリスチレン系樹脂ペレットは、押
出機において、ポリスチレン系樹脂、顔料等を練り込
み、着色された樹脂をストランド状で、引き取り、ペレ
タイザーでカットし、着色発泡性ポリスチレンペレット
を得て、予備発泡して予備発泡粒子を得る。等の方法が
行われていた。そして、これらの予備発泡された予備発
泡粒子を成形型に充填し、発泡成形を行い得られてい
た。
2. Description of the Related Art Conventionally, as a method for obtaining pre-expanded particles of colored expandable particles, a colorant such as a pigment or a dye is uniformly coated on a surface of expandable polystyrene particles by a Henschel mixer or a ribbon blender.
The pre-expanded colored foamable particles obtained in this manner are pre-expanded to obtain pre-expanded particles. The polystyrene particles are uniformly stirred in an aqueous medium, a foaming agent is press-fitted, an oil-soluble dye or the like is charged, and a colorant is impregnated into the particles to obtain colored foamable polystyrene particles, which are pre-foamed. To obtain pre-expanded particles. In the extruder, the colored foamable polystyrene resin pellets are kneaded with a polystyrene resin, a pigment, and the like, and the colored resin is taken out in a strand shape, cut with a pelletizer, to obtain a colored foamable polystyrene pellet, and prefoamed. To obtain pre-expanded particles. And so on. Then, these pre-expanded pre-expanded particles are filled in a mold and subjected to foam molding.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、 方
法においては、予備発泡粒子の表面のみが着色されたて
いるために、これを用いて成形品を得ると、この成形品
をカットすると、カット面は着色されていない部分があ
り、また表面部分の色むらも発生し易いものであった。
また、の方法では、粒子内部まで、着色剤は、含浸さ
れるが、全体に均一に成らず、これを均一に着色するた
めには、着色剤を多量に使用し、さらに着色剤の含浸時
間を長くする必要があり、これにより、反応容器等の汚
染や、排水の汚染を引き起こす恐れがあり、さたに、作
業能率の低下となる。さらにまたの方法では、着色発
泡性ポリスチレン系樹脂ペレット内部は均一着色されて
いるが、成形品の表面において、色むらが発生してしま
う。これは、この着色発泡性ポリスチレン系樹脂ペレッ
トを予備発泡すると、予備発泡粒子表面の長さ方向と、
カット面とでは、セルの状態が異なり、カット面のセル
が微細となり、そのために、色むらが発生し、カット面
の色が長さ方向の色より薄くなってしまう。この予備発
泡粒子を成形型に充填し、発泡成形して得られた成形品
は、色むらがあり、外観が良くないものであった。さら
に、黒のような濃色なほど、色むらが明確になってしま
った。また、発泡粒子間の密着性がよくない、粒子間隙
の多い成形品であった。本発明は、これらの問題を背景
になされたのであり、色むらのより少ない、粒子間隙の
殆どない、成形品を得るための予備発泡粒子を提供する
ことを目的とする。
However, in the method, since only the surface of the pre-expanded particles is colored, when a molded article is obtained by using this, when this molded article is cut, the cut surface becomes There were uncolored portions, and color unevenness of the surface portion was liable to occur.
In the method of (1), the coloring agent is impregnated up to the inside of the particles, but is not uniform over the entire surface. In order to uniformly color the coloring agent, a large amount of the coloring agent is used, and the impregnation time of the coloring agent It is necessary to increase the length of time, which may cause contamination of the reaction vessel and the like and contamination of the wastewater, and further reduce the work efficiency. According to the further method, the inside of the colored expandable polystyrene resin pellet is uniformly colored, but color unevenness occurs on the surface of the molded product. This is because when the colored expandable polystyrene resin pellets are pre-expanded, the length direction of the surface of the pre-expanded particles,
The state of the cells differs from that of the cut surface, and the cells of the cut surface become finer, so that color unevenness occurs and the color of the cut surface becomes lighter than the color in the length direction. A molded article obtained by filling the pre-expanded particles into a molding die and foam-forming had uneven color and poor appearance. Further, the darker the color, such as black, the more the color unevenness became clear. In addition, the molded article had poor adhesion between the expanded particles and had many interparticle gaps. The present invention has been made in view of these problems, and an object of the present invention is to provide pre-expanded particles for obtaining a molded article having less color unevenness and almost no particle gap.

【0004】[0004]

【課題を解決するための手段】本発明者は、着色された
予備発泡粒子が、成形型に充填されるときに、成形型表
面にそって、配向するのは、予備発泡粒子の長さ方向と
カット面との何れか、長さの長い方となり、この配向が
一定になるようし、更に色が濃い長さ方向を長径とし、
カット面を短径とすることで、成形型表面に、予備発泡
粒子は、長径が配向する確率が大きく、色むらのより少
ない成形品を得られることを見出し、ここに本発明を完
成するに至った。
SUMMARY OF THE INVENTION The present inventors have determined that when the colored pre-expanded particles are filled in the mold, they are oriented along the surface of the mold in the longitudinal direction of the pre-expanded particles. Either the cut surface or the cut surface will be the longer one, and this orientation will be constant, and the longer color direction will be the longer diameter,
By making the cut surface a short diameter, the pre-expanded particles on the mold surface have a high probability that the long diameter is oriented, and it is found that a molded article with less color unevenness can be obtained, and here the present invention is completed. Reached.

【0005】本発明は、発泡性ポリスチレン系樹脂ペレ
ットを予備発泡してなる粒子であって、予備発泡粒子の
長径lと短径dの比が1<l/d≦4であることを特徴
とする予備発泡粒子を提供するものである。また、本発
明は、発泡性ポリスチレン系樹脂ペレットが着色されて
いることを特徴とする予備発泡粒子を提供するものであ
る。さらに本発明は、着色発泡性ポリスチレン系樹脂ペ
レットの長径Lと短径Dとの比L/Dが5〜30である
ことを特徴とする着色発泡性ポリスチレン系樹脂ペレッ
トを提供するものである。
The present invention is a particle obtained by pre-expanding expandable polystyrene resin pellets, wherein the ratio of the major axis l to the minor axis d is 1 <l / d ≦ 4. To provide pre-expanded particles. The present invention also provides pre-expanded particles characterized in that expandable polystyrene resin pellets are colored. Further, the present invention provides a colored expandable polystyrene resin pellet, wherein the ratio L / D of the major axis L and the minor axis D of the colored expandable polystyrene resin pellet is 5 to 30.

【0006】[0006]

【発明の実施の形態】本発明の予備発泡粒子は、発泡性
ポリスチレン系樹脂ペレットの長さ方向を長径L,カッ
ト面を短径Dとして、これを通常の予備発泡して、該ペ
レットを約10〜50倍に発泡させて、変化した長径L
を予備発泡粒子の長径lとし、また、変化した短径Dを
予備発泡粒子の短径dとした。この長径lと短径dの長
さの比を1<l/d≦4をとした。この比がl/dが1
以下であると、成形品に色むらの発生が多くなり、l/
dが4以上であると色むらの発生は少ないが、成形型の
充填孔に詰まって、充填不良になったり、成形品の粒子
間隙の発生が起こりやすくなる。したがって、長径l
は、成形型への充填性を考慮すると、成形型の充填孔を
Wとすると、W≧3lの長さの関係にあることが好まし
い。W<3lであると、充填孔に予備発泡粒子が詰まり
易くなりやすい。
BEST MODE FOR CARRYING OUT THE INVENTION The pre-expanded particles of the present invention are prepared by ordinary pre-expanding the expandable polystyrene resin pellets in the length direction as a major axis L and a cut surface as a minor axis D, and the pellets are reduced to about Foamed 10 to 50 times, changed long diameter L
Is the major axis 1 of the pre-expanded particles, and the changed minor axis D is the minor axis d of the pre-expanded particles. The ratio of the length of the major axis 1 to the minor axis d was set to 1 <l / d ≦ 4. This ratio is 1 / d
If it is less than 1, the occurrence of color unevenness in the molded article increases, and 1 /
When d is 4 or more, the occurrence of color unevenness is small, but clogging of the filling hole of the molding die causes poor filling, and the occurrence of particle gaps in the molded product tends to occur. Therefore, the major axis l
In consideration of the filling property of the mold, it is preferable that the length of the mold is W ≧ 31, where W is the filling hole of the mold. If W <31, the pre-expanded particles are likely to be clogged in the filling holes.

【0007】本発明における予備発泡粒子を得るため
に、着色発泡性ポリスチレン系樹脂ペレットの長径Lと
短径Dの長さの比がL/Dが5〜30であることが望ま
しい。この長さの比がL/Dが5未満であると、通常の
予備発泡を行なった場合、本発明の予備発泡粒子を得る
ことができにくい、長さの比がL/Dが30を超える
と、予備発泡段階で、ペレットが、細長くなりすぎて、
成形型の充填孔に詰まりやすくなり、充填不良の原因と
なる恐れがある。そのために、着色発泡性ポリスチレン
系樹脂ペレットの長径Lと短径Dの長さの比がL/Dが
5〜30の範囲内であるように、予備発泡前の段階で、
分粒しておくことが望ましい。
In order to obtain the pre-expanded particles in the present invention, it is desirable that the ratio L / D of the major axis L to the minor axis D of the colored expandable polystyrene resin pellets is 5 to 30. When the length ratio is less than 5, the pre-expanded particles of the present invention are difficult to obtain when ordinary pre-expansion is performed. The length ratio L / D exceeds 30. And, in the pre-foaming stage, the pellets are too elongated,
The filling hole of the molding die is likely to be clogged, which may cause defective filling. Therefore, at the stage before pre-foaming, the ratio of the length L of the major axis L to the minor axis D of the colored expandable polystyrene resin pellet is in the range of 5 to 30.
It is desirable to sizing.

【0008】次に、本発明の発泡性ポリスチレン系樹脂
ペレットの予備発泡粒子の製造方法ついて説明する。例
えば、揮発性発泡剤を含んだポリスチレン系樹脂及び必
要に応じて、ブレンド樹脂と染料、顔料などの着色剤並
びにその他の添加剤を一緒に、予め、ヘンシェルミキサ
ーやリボンブレンダー等により均一にブレンドした後
に、押出機内に投入し、これを、加熱による溶融そして
スクリューによる混練に続いて、ダイス先端より樹脂を
押し出し、直ちに水槽で冷却する。この時に、ダイス先
端より押し出した樹脂が発泡しないうちに冷却するよう
に注意する必要がある。そして、ストランド状に引き取
り、その後、そのストランドをロータリー式ペレタイザ
ー等において、所望長さのLに切断し、長径Lで短径D
の着色発泡性ポリスチレン系樹脂ペレットを得る。
Next, a method for producing pre-expanded particles of expandable polystyrene resin pellets of the present invention will be described. For example, a polystyrene-based resin containing a volatile foaming agent and, if necessary, a blended resin and a colorant such as a dye or a pigment and other additives were previously uniformly blended with a Henschel mixer or a ribbon blender in advance. Thereafter, the resin is put into an extruder, and after being melted by heating and kneaded by a screw, the resin is extruded from the tip of the die and immediately cooled in a water tank. At this time, care must be taken to cool the resin extruded from the die tip before foaming. Then, the strand is taken up in a strand shape, and then the strand is cut into a desired length L by a rotary pelletizer or the like.
To obtain colored foamable polystyrene resin pellets of

【0009】この得られた着色発泡性ポリスチレン系樹
脂ペレットを、通常の予備発泡法によって、約10〜6
0倍の嵩倍率にして、本発明の長径lで、短径dの比が
1<l/d≦4の予備発泡粒子を得ることができる。ま
た、本発明の予備発泡粒子の製造においては、発泡性ポ
リスチレン系樹脂ペレットを製造するには、押し出し含
浸法のように、押出機内で樹脂を溶融した後または最中
に、揮発性発泡剤を圧入して、溶融状態にある樹脂と十
分に混合したのちに、ストランドの形態に押し出して、
直ちに水槽で冷却する。この時に、ダイス先端より押し
出した樹脂が発泡しないうちに冷却するように注意する
必要がある。その後、そのストランドをロータリー式ペ
レタイザー等において、所望長さのLに切断し、長径L
で短径Dの発泡性ポリスチレン系樹脂ペレットを得ても
よい。
The obtained colored expandable polystyrene resin pellets are prepared by a conventional pre-expansion method by about 10-6.
By setting the bulk ratio to 0, pre-expanded particles having a major axis l and a minor axis d ratio of 1 <l / d ≦ 4 according to the present invention can be obtained. In the production of the pre-expanded particles of the present invention, in order to produce expandable polystyrene resin pellets, as in the extrusion impregnation method, after or during melting of the resin in an extruder, a volatile foaming agent is used. After press-fitting and thoroughly mixing with the resin in the molten state, it is extruded into the form of a strand,
Cool immediately in a water bath. At this time, care must be taken to cool the resin extruded from the die tip before foaming. Thereafter, the strand is cut into L having a desired length with a rotary pelletizer or the like, and the long diameter L is cut.
To obtain an expandable polystyrene resin pellet having a short diameter D.

【0010】本発明においては、予備発泡粒子が、長径
lで、短径dの比が1<l/d≦4の関係をしていれば
よく、また、好ましくは、発泡性ポリスチレン系樹脂ペ
レットの長径Lと短径Dとの比L/Dが5〜30である
ものであればよく、いかなる製造方法によって得られた
ものでもよい。また、成形型の充填孔の直径をWとする
と、予備発泡粒子の長径lが3l≦Wの関係になってい
ることが好ましい、W<3lであると、予備発泡粒子
が、充填孔に詰まりやすくなり、作業性の面で好ましく
ない。
In the present invention, the pre-expanded particles only need to have a relation of a major axis l and a minor axis d of 1 <l / d ≦ 4, and preferably, expandable polystyrene resin pellets. The ratio L / D of the major axis L and the minor axis D may be 5 to 30 and may be obtained by any manufacturing method. Further, assuming that the diameter of the filling hole of the mold is W, it is preferable that the major diameter l of the pre-expanded particles is in a relationship of 3l ≦ W. If W <3l, the pre-expanded particles are clogged in the filling hole. This is not preferable in terms of workability.

【0011】本発明でいうポリスチレン系樹脂とは、ス
チレン系単量体の単独重合体に限らず、他の単量体との
共重合体(スチレン系単量体を50%以上の割合で使用
して作られる)を含む。従って、本発明に用いるスチレ
ン系樹脂としては、ポリスチレンの他、ポリαーメチル
スチレン、ポリpークロロスチレン等のポリスチレンの
他、スチレンと置換スチレン(例えばαーメチルスチレ
ン等)との共重合体、あるいは、スチレンとビニル系単
量体(例えばアクリルニトリル)との共重合体等が挙げ
られる。また、前記のポリスチレン系樹脂に、ポニフェ
ニルエーテル系樹脂やポリオレフィン系樹脂、及びゴム
成分等をブレンドして、発泡性樹脂としての物性を改良
した樹脂も本発明のポリスチレン系樹脂とすることがで
きる。
The polystyrene resin referred to in the present invention is not limited to a homopolymer of a styrene monomer, but may be a copolymer with another monomer (a styrene monomer used in a proportion of 50% or more). Made). Accordingly, the styrene resin used in the present invention includes, in addition to polystyrene, polystyrene such as poly-α-methylstyrene and poly-p-chlorostyrene, a copolymer of styrene and a substituted styrene (for example, α-methylstyrene), or styrene and vinyl. Copolymers with a system monomer (for example, acrylonitrile) are exemplified. Further, the polystyrene resin of the present invention can also be a resin obtained by blending a polyphenyl ether resin or a polyolefin resin, a rubber component, or the like with the polystyrene resin, and improving the physical properties of the foamable resin. .

【0012】本発明で使用される、着色剤は、カーボン
ブラック、酸化チタン、亜鉛華、硫化亜鉛、酸化アンチ
モン、黄鉛、べんがら、酸化鉄、群青等の無機系のも
の、銅フタロシアニンブルー、ハンザイエロー、ピアゾ
ロンレッド、パーマネントボルドー等の有機系のものが
ある。また、水溶性のものより、難水溶性の顔料の方が
本発明に着色剤として好ましい。
The colorants used in the present invention include inorganic materials such as carbon black, titanium oxide, zinc white, zinc sulfide, antimony oxide, graphite, red iron oxide, ultramarine blue, copper phthalocyanine blue, Hansa There are organic ones such as yellow, piazolone red and permanent bordeaux. In addition, poorly water-soluble pigments are more preferable as colorants in the present invention than water-soluble pigments.

【0013】本発明で用いられる揮発性発泡剤として、
常圧における沸点が、−30℃〜100℃の範囲にある
もので、例えば、プロパン、n−ブタン、i−ブタン、
n−ペンタン、i−ぺンタン、ヘキサン、ヘプタン等の
脂肪族炭化水素、及び環状脂肪族炭化水素、ハロゲン化
炭化水素類等を使用することができる。また、これらの
2種類または3種類以上を併用して使用することもでき
る。この揮発性発泡剤を予め含有したポリスチレン系樹
脂を押出機に投入しても、押出機にポリスチレン樹脂等
を投入後に揮発性発泡剤を圧入してもよい。
As the volatile foaming agent used in the present invention,
Boiling point at normal pressure is in the range of −30 ° C. to 100 ° C., for example, propane, n-butane, i-butane,
Aliphatic hydrocarbons such as n-pentane, i-pentane, hexane, heptane and the like, and cycloaliphatic hydrocarbons, halogenated hydrocarbons and the like can be used. Two or more of these can be used in combination. The polystyrene-based resin containing the volatile foaming agent in advance may be charged into the extruder, or the volatile foaming agent may be press-fitted after the polystyrene resin or the like is charged into the extruder.

【0014】[0014]

【作用】本発明の予備発泡粒子を発泡成形に使用するこ
とにより、成形型に充填時に予備発泡粒子が成形型の表
面に一定に配向されるので、色むらのほとんどない発泡
成形品をえることができ、さらに、発泡粒子間の隙間の
少ない成形品を得ることができる。また、発泡性ポリス
チレン系樹脂ペレットの長径と短径の比、予備発泡粒子
の長径と短径の比とが、一定の範囲に決定されているた
めに、成形型への充填性等の作業性の向上を計ることが
可能となる。
By using the pre-expanded particles of the present invention for foam molding, since the pre-expanded particles are uniformly oriented on the surface of the mold when filling the mold, it is possible to obtain a foam molded article having almost no color unevenness. In addition, it is possible to obtain a molded article having few gaps between the foamed particles. In addition, since the ratio of the major axis to the minor axis of the expandable polystyrene resin pellets and the ratio of the major axis to the minor axis of the pre-expanded particles are determined within a certain range, the workability such as the filling property into the molding die is improved. Can be improved.

【0015】[0015]

【実施例】以下、実施例を挙げ、本発明をさらに具体的
に説明するが、本発明は、これらの実施例に限定される
ものではない。 実施例1 nーペンタンを樹脂に対して10重量%含有した発泡性
ポリスチレン樹脂100重量部、着色剤としてカーボン
ブラックを5重量部、ステアリン酸亜鉛0.1重量部を
リボンブレンダーで、均一に混合し、この混合物を単軸
押出機3内に一緒に投入し、原料投入部の温度を100
℃、溶融部を140℃として、溶融させて、スクリュー
にて混練し、口金0.8mmのダイス4よりストランド
状6にて押し出し、これを直ちに水8にて冷却したの
ち、ストランド状6に引き取り、そのストランドをロタ
リー式ペレタイザー9において、長さ平均4mm,太さ
平均0.4mmの着色発泡性ポリスチレン樹脂ペレット
2を得た。この得られた発泡性ポリスチレン樹脂ペレッ
トを通常の予備発泡方法により、嵩倍率30倍の長径
3.2mm,短径3.0mmの予備発泡粒子1を得た。
EXAMPLES The present invention will now be described in more detail with reference to examples, but the present invention is not limited to these examples. Example 1 100 parts by weight of an expandable polystyrene resin containing 10% by weight of n-pentane with respect to the resin, 5 parts by weight of carbon black as a coloring agent, and 0.1 part by weight of zinc stearate were uniformly mixed by a ribbon blender. This mixture was put into the single screw extruder 3 together, and the temperature of the raw material charging section was set to 100
C., the melting portion was set to 140 ° C., the mixture was melted, kneaded with a screw, extruded in a strand shape 6 from a die 4 having a base of 0.8 mm, cooled immediately with water 8, and then taken up in a strand shape 6. The strands were subjected to a rotary type pelletizer 9 to obtain colored foamable polystyrene resin pellets 2 having an average length of 4 mm and an average thickness of 0.4 mm. The obtained expandable polystyrene resin pellets were subjected to a normal pre-expansion method to obtain pre-expanded particles 1 having a major axis of 30 times and a major axis of 3.2 mm and a minor axis of 3.0 mm.

【0016】実施例2 実施例1と同様に長径4.0mm、短径0.4mmの発
泡性ポリスチレン樹脂ペレットを得て、予備発泡におい
て、嵩倍率15倍の長径2.6mm,短径2.3mmの
予備発泡粒子を得た。
Example 2 In the same manner as in Example 1, expandable polystyrene resin pellets having a major axis of 4.0 mm and a minor axis of 0.4 mm were obtained. 3 mm of pre-expanded particles were obtained.

【0017】比較例1 実施例1と同様に長径2.3mm、短径0.55mmの
発泡性ポリスチレン樹脂ペレットを得て、予備発泡にお
いて、嵩倍率30倍の長径4.0mm,短径3.5mm
の予備発泡粒子を得た。
Comparative Example 1 In the same manner as in Example 1, expandable polystyrene resin pellets having a major axis of 2.3 mm and a minor axis of 0.55 mm were obtained. 5mm
Of pre-expanded particles were obtained.

【0018】比較例2 実施例1と同様に長径2.0mm、短径0.50mmの
発泡性ポリスチレン樹脂ペレットを得て、予備発泡にお
いて、嵩倍率40倍の長径3.3mm,短径3.5mm
の予備発泡粒子を得た。
Comparative Example 2 In the same manner as in Example 1, expandable polystyrene resin pellets having a major axis of 2.0 mm and a minor axis of 0.50 mm were obtained. 5mm
Of pre-expanded particles were obtained.

【0019】各実施例、比較例で作成された、予備発泡
粒子を、室温にて12時間熟成し、充填孔の直径10m
mを有する成形型に投入し、蒸気圧力(ゲージ圧)0.
8kg/cm3 にて30秒間加熱する発泡成形を行い、
50mm×300mm×300mmの大きさの発泡成形
品をつくった。成形型への予備発泡粒子の充填性、成形
品の色むら、粒子間隙の評価を行った。その結果を表1
に示す。
The pre-expanded particles prepared in each of Examples and Comparative Examples were aged at room temperature for 12 hours, and the diameter of the filling hole was 10 m.
m and a steam pressure (gauge pressure) of 0.
Perform foam molding by heating at 8 kg / cm 3 for 30 seconds.
A foam molded product having a size of 50 mm × 300 mm × 300 mm was produced. The filling property of the pre-expanded particles into the mold, the color unevenness of the molded product, and the particle gap were evaluated. Table 1 shows the results.
Shown in

【0020】 注)表1中のl:予備発泡粒子の長径 d:予備発泡粒子の短径 W:成形型の充填孔の直径[0020] Note) 1 in Table 1: major diameter of pre-expanded particles d: minor diameter of pre-expanded particles W: diameter of filling hole of mold

【0021】実施例1、2においては、l/dが1以上
であり、W>3lであるために、色むらもなく、粒子間
隙も少なく成形品を得ることができ、さらに、成形型へ
の充填作業性も問題のないものであった。比較例1にお
いては、l/dが1以上であるが、W<3lであるため
に、成形品においては色むら等の発生はないが、成形型
への充填性に問題があった。また、比較例2において
は、l/dが1未満であるために、成形品の色むら及び
粒子間隙の発生があり、成形品としての品質に問題があ
った。
In Examples 1 and 2, since l / d is 1 or more and W> 31, a molded article without color unevenness and with a small particle gap can be obtained. The filling workability was also satisfactory. In Comparative Example 1, although l / d was 1 or more, since W <31, there was no occurrence of color unevenness or the like in the molded product, but there was a problem in the filling property into the molding die. Further, in Comparative Example 2, since l / d was less than 1, color unevenness and particle gap of the molded product occurred, and there was a problem in the quality of the molded product.

【0022】[0022]

【発明の効果】本発明においては、予備発泡粒子の長径
と短径の比率を規定することにより、成形型の成形面に
おいて、予備発泡粒子の配向性を持たせるために、色む
らの発生が起こりにくく、粒子間隙も少ない成形品を得
ることができる。成形型の充填孔の大きさにより、予備
発泡粒子の長径を決定することにより、充填孔に予備発
泡粒子が詰まること無く、自動成形機などにおける、充
填不良による成形品の不良の発生を防止できる。
According to the present invention, since the ratio of the major axis to the minor axis of the pre-expanded particles is specified, the unevenness of the color of the pre-expanded particles is generated on the molding surface of the mold so that the pre-expanded particles have orientation. It is possible to obtain a molded product that hardly occurs and has a small particle gap. By determining the major diameter of the pre-expanded particles according to the size of the filling hole of the mold, it is possible to prevent the occurrence of defective molded products due to defective filling in an automatic molding machine or the like without filling the filled holes with the pre-expanded particles. .

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

【図1】 実施例の予備発泡粒子の斜視図FIG. 1 is a perspective view of pre-expanded particles of an example.

【図2】 実施例の着色発泡性ポリスチレン系樹脂ペ
レットの斜視図
FIG. 2 is a perspective view of a colored expandable polystyrene resin pellet of an example.

【図3】 実施例の着色発泡性ポリスチレン系樹脂ペ
レットの製造工程図
FIG. 3 is a production process diagram of a colored expandable polystyrene resin pellet of an example.

【符号の説明】[Explanation of symbols]

1 着色発泡性ポリスチレン系樹脂ペレット 2 予備発泡粒子 3 押出機 5 ダイス放出部 6 ストランド 7 ストランド引き取りローラー 8 水 9 ペレタイザー DESCRIPTION OF SYMBOLS 1 Colored expandable polystyrene resin pellet 2 Pre-expanded particle 3 Extruder 5 Die discharge part 6 Strand 7 Strand take-up roller 8 Water 9 Pelletizer

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C08L 25:04 ──────────────────────────────────────────────────の Continued on front page (51) Int.Cl. 6 Identification code FI C08L 25:04

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 発泡性ポリスチレン系樹脂ペレットを予
備発泡してなる粒子であって、予備発泡粒子の長径lと
短径dの比が1<l/d≦4であることを特徴とする予
備発泡粒子。
1. A pre-expanded particle obtained by pre-expanding expandable polystyrene resin pellets, wherein the ratio of the major axis l to the minor axis d is 1 <l / d ≦ 4. Expanded particles.
【請求項2】 発泡性ポリスチレン系樹脂ペレットが着
色されていることを特徴とする請求項1記載の予備発泡
粒子。
2. The pre-expanded particles according to claim 1, wherein the expandable polystyrene resin pellets are colored.
【請求項3】 着色発泡性ポリスチレン系樹脂ペレット
の長径Lと短径Dとの比L/Dが5〜30であることを
特徴とする着色発泡性ポリスチレン系樹脂ペレット。
3. A colored foamable polystyrene resin pellet, wherein the ratio L / D of the major axis L and the minor axis D of the colored foamable polystyrene resin pellet is 5 to 30.
JP9203869A 1997-07-14 1997-07-14 Preexpanded particle Pending JPH1135731A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9203869A JPH1135731A (en) 1997-07-14 1997-07-14 Preexpanded particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9203869A JPH1135731A (en) 1997-07-14 1997-07-14 Preexpanded particle

Publications (1)

Publication Number Publication Date
JPH1135731A true JPH1135731A (en) 1999-02-09

Family

ID=16481065

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9203869A Pending JPH1135731A (en) 1997-07-14 1997-07-14 Preexpanded particle

Country Status (1)

Country Link
JP (1) JPH1135731A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010229205A (en) * 2009-03-26 2010-10-14 Sekisui Plastics Co Ltd Expandable thermoplastic resin particle, process for producing the same, prefoamed particle and foam molded product

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010229205A (en) * 2009-03-26 2010-10-14 Sekisui Plastics Co Ltd Expandable thermoplastic resin particle, process for producing the same, prefoamed particle and foam molded product

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