JP3221019B2 - Low-density fused expanded resin molded article of polystyrene resin expanded particles and method for producing the same - Google Patents

Low-density fused expanded resin molded article of polystyrene resin expanded particles and method for producing the same

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Publication number
JP3221019B2
JP3221019B2 JP30833891A JP30833891A JP3221019B2 JP 3221019 B2 JP3221019 B2 JP 3221019B2 JP 30833891 A JP30833891 A JP 30833891A JP 30833891 A JP30833891 A JP 30833891A JP 3221019 B2 JP3221019 B2 JP 3221019B2
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JP
Japan
Prior art keywords
particles
resin
polystyrene
foamed
rubber
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 - Fee Related
Application number
JP30833891A
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Japanese (ja)
Other versions
JPH05116227A (en
Inventor
勲 木葉
学 田沼
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.)
Asahi Kasei Corp
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Asahi Kasei Corp
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Priority to JP30833891A priority Critical patent/JP3221019B2/en
Publication of JPH05116227A publication Critical patent/JPH05116227A/en
Application granted granted Critical
Publication of JP3221019B2 publication Critical patent/JP3221019B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

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

【0001】[0001]

【産業上の利用分野】本発明は、ゴム変性ポリスチレン
系樹脂発泡粒子の低密度融着発泡樹脂成形体とその製造
方法に関する。本発明によれば電子部品,音響機器等が
著しく小型化、軽量化され、増々軽量物の緩衝包装材の
要求が高まる中で、特に軽量物に対する緩衝性能に優れ
て、かつ近年社会問題となっているプラスチックの産業
廃棄物への対応から従来品よりもはるかに低密度なるが
ゆえに従来の緩衝材料よりも大巾に使用重量を低減出来
る結果、産業廃棄物の発生量を削減出来る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a low-density fused foamed resin molded article of rubber-modified polystyrene resin foamed particles and a method for producing the same. According to the present invention, electronic components, audio equipment, and the like are significantly reduced in size and weight, and the demand for cushioning packaging materials for lighter objects is increasing. Since the density of plastics is much lower than that of conventional products due to the handling of industrial waste, the weight used can be greatly reduced as compared with conventional buffer materials. As a result, the amount of industrial waste generated can be reduced.

【0002】[0002]

【従来の技術】従来から軽量の被包装物を硬くて弾性に
乏しいポリスチレンン系樹脂発泡粒子の融着発泡成形体
(以下、発泡成形体と称す)による緩衝材で緩衝包装し
た場合、硬すぎて、十分なる緩衝吸収効果が得れないと
いう問題があった。その解決手段として従来より、通称
ハイインパクトポリスチレン樹脂と称されているポリス
チレンの連続相にポリスチレンが単数又は複数の小粒子
状に内包されたブタジエン系重合体ゴムが粒子状に分散
してなるゴム変性ポリスチレン樹脂を用いて発泡粒子を
得て発泡成形体を得ることは知られている。
2. Description of the Related Art Conventionally, when a light-weight packaged article is cushioned and packaged with a cushioning material made of a fused foamed molded article of foamed polystyrene resin particles having a low elasticity and poor elasticity (hereinafter referred to as a foamed molded article), it is too hard. Thus, there is a problem that a sufficient buffer absorption effect cannot be obtained. As a solution to this, a rubber-modified rubber in which a butadiene-based polymer rubber in which polystyrene is encapsulated in one or more small particles in a continuous phase of polystyrene, commonly called a high-impact polystyrene resin, is dispersed in the form of particles. It is known to obtain expanded molded articles by obtaining expanded particles using a polystyrene resin.

【0003】例えば、特公昭51−46536号公報に
は、ポリスチレン樹脂に、ブタジエン成分が加わる事で
得られる発泡成形体の弾性を高められる事が、又、特開
昭56−67344号公報には、平均ゴム粒子径を0.
7μm以下に調整することでさらに耐衝撃性能を高める
ことが開示されている。しかしながら上記発明で言う
「耐衝撃破壊性能」とは主に発泡成形体が落下衝撃によ
って割れたり、折れたりすることを防止する性能であっ
て、本発明で言う、気泡膜が非常に薄膜状にある低密度
発泡成形体に特有な現象である気泡があたかもパンクす
るが如く破裂するのを防止する「耐気泡のパンク防止性
能」と明らかに異るものである。
[0003] For example, Japanese Patent Publication No. 51-46536 discloses that the elasticity of a foamed molded article obtained by adding a butadiene component to a polystyrene resin can be enhanced. , The average rubber particle diameter is 0.1.
It is disclosed that the impact resistance can be further improved by adjusting the thickness to 7 μm or less. However, the "impact destruction performance" referred to in the above invention is a performance mainly for preventing the foamed molded article from being broken or broken by a drop impact, and the foam film in the present invention is very thin. This is clearly different from the “bubble-resistant puncture-preventing performance” of preventing bubbles that are a phenomenon peculiar to a certain low-density foam molded article from bursting as if they were punctured.

【0004】又ブタジエン成分を加えることによって得
られる発泡成形体の弾性を改善出来たとは言え高発泡性
能が劣り、弾性を高める上で、ブタジエン成分を加える
事にも増して重要な要因である発泡成形体の低密度化の
達成が充分で無く、結果として得られる発泡成形体を軽
量物の緩衝包装材に用いた時、十分なる緩衝効果を得ら
れないという問題があった。
[0004] Although the elasticity of the foamed article obtained by adding the butadiene component can be improved, the high foaming performance is inferior, and foaming, which is an important factor in increasing the elasticity, is more important than the addition of the butadiene component. There has been a problem that the density of the molded article has not been sufficiently reduced, and when the resulting foam molded article is used as a lightweight cushioning packaging material, a sufficient cushioning effect cannot be obtained.

【0005】[0005]

【発明が解決しようとする課題】一般に電子部品や音響
機器等の軽量製品は、緩衝包装する際、緩衝材となる発
泡成形体に加わる受圧荷重が小さく(すなわち低応力)
となるため落下衝撃に対し発泡成形体の圧縮変形が小さ
くとどまり、衝撃吸収効果が充分得られにくいという問
題があり、軽量物に対する緩衝性能、いわゆる「低応力
衝撃吸収性能」に優れて、かつポリスチレン系樹脂発泡
成形体による経済性の高い軽量物用緩衝包装材の完成が
強く望まれている。
Generally, when a light-weight product such as an electronic component or an audio device is subjected to cushioning and packaging, a pressure-receiving load applied to a foamed molded article serving as a cushioning material is small (that is, low stress).
Therefore, there is a problem that the compression deformation of the foamed molded article is small in response to a drop impact, and it is difficult to sufficiently obtain an impact absorbing effect. There is a strong demand for a highly economical lightweight cushioning packaging material using a resin foam molded article.

【0006】本発明者らは、ポリスチレン樹脂にゴム成
分を加える事によって、基本的な緩衝性能である、衝撃
吸収性能の持続性を示すところの「圧縮歪の回復性能」
と、通称「パンク現象」と言われる、落下衝撃によって
発生する発泡成形体を構成する気泡膜の破裂を防止する
ところの「耐気泡のパンク防止性能」を備えることに加
え、ゴム成分を加える事で、著しく高発泡性能が低下す
る性状を改善し、従来品より高度に低密度の発泡成形体
を得る事を可能にして、これまでポリスチレンン系樹脂
発泡成形体では不可能と思われたレベルの、高い弾性を
もった発泡成形体を完成しようとするものである。
By adding a rubber component to a polystyrene resin, the inventors of the present invention have shown a "compression strain recovery performance" which shows the continuity of shock absorption performance, which is the basic buffering performance.
In addition to having the "puncture resistance of air bubbles" that prevents the rupture of the foam film that constitutes the foam molded article caused by the drop impact, commonly called the "puncture phenomenon", and adding a rubber component In this way, it is possible to improve the property that the high foaming performance is remarkably reduced, and to obtain a foam molded article with a higher density than conventional products, a level that was thought to be impossible with polystyrene resin foam molded articles so far. However, it is intended to complete a foamed molded article having high elasticity.

【0007】[0007]

【課題を解決するための手段】本発明は、ポリスチレン
の連続相に、内部にポリスチレンが小粒子状に内包され
たブタジエン系重合体ゴムが粒子状に分散しており、全
体に占めるブタジエン成分の含有量が5〜15重量
あり、かつブタジエン系重合体ゴム粒子の重量平均粒子
径が0.05〜1.0μmでその粒子径分布が1.5以
下であるゴム変性ポリスチレン樹脂の発泡粒子からなる
成形体であって、その密度が0.009〜0.014g
/cm3 であり、かつその気泡の80%以上が独立気泡
構造を有するポリスチレン系樹脂発泡粒子の低密度融着
発泡樹脂成形体、及びポリスチレンの連続相に内部にポ
リスレンが小粒子状に内包されたブタジエン系重合体ゴ
ムが粒子状に分散しており、全体に占めるブタジエン成
分の含有量が5〜15重量%であり、かつブタジエン系
重合体ゴム粒子の重量平均粒子径が0.05〜1.0μ
mでその粒子径分布が1.5以下であるゴム変性ポリス
チレン樹脂100グラム量について揮発性有機発泡剤を
0.07〜0.25グラムモル量を含浸し、発泡性樹脂
粒子を得て後、該発泡性樹脂粒子を発泡機内でスチーム
によって発泡し1回の発泡で嵩密度が0.009〜0.
014g/ccの発泡粒子を得、ついで該発泡粒子を成
形型に導入しスチームで加熱し発泡粒子相互を融着成形
して、その密度が0.009〜0.014g/cm
3 で、かつその気泡の80%以上が独立気泡構造を有す
るポリスチレン系樹脂発泡粒子の低密度融着発泡樹脂成
形体の製造方法であり、本発明によって前記課題は容易
に達成出来る。
According to the present invention, a butadiene polymer rubber in which polystyrene is encapsulated in small particles is dispersed in a continuous phase of polystyrene in the form of particles. Expanded rubber-modified polystyrene resin particles having a content of 5 to 15 % by weight and a weight average particle diameter of the butadiene polymer rubber particles of 0.05 to 1.0 μm and a particle diameter distribution of 1.5 or less. A molded article having a density of 0.009 to 0.014 g
/ Cm 3 , and 80% or more of the cells have a closed cell structure, and a low-density fusion-foamed resin molded article of polystyrene-based resin expanded particles, and polystyrene is contained in small particles in a continuous phase of polystyrene. Butadiene-based polymer rubber is dispersed in the form of particles, the content of the butadiene component in the whole is 5 to 15% by weight, and the weight-average particle size of the butadiene-based polymer rubber particles is 0.05 to 1%. 0.0μ
m, a volatile organic blowing agent is impregnated with 0.07 to 0.25 gmol in an amount of 100 g of a rubber-modified polystyrene resin having a particle size distribution of 1.5 or less to obtain expandable resin particles. The foamable resin particles are foamed with steam in a foaming machine, and the bulk density is 0.009 to 0.1 in one foaming.
014 g / cc of foamed particles were obtained, and then the foamed particles were introduced into a mold, heated with steam to fuse and form the foamed particles, and the density was 0.009 to 0.014 g / cm.
3 , and 80% or more of the cells are a method for producing a low-density fused foamed resin molded article of polystyrene resin foamed particles having a closed cell structure, and the above object can be easily achieved by the present invention.

【0008】本発明で言うゴム変性ポリスチレンは、ブ
タジエン系重合体としてのポリブタジン又はブタジエ
ン−スチレン共重合体をスチレンモノマーに溶解し、重
合液となす、次いで該重合液を加熱し撹拌しつつ重合し
ブタジエン系重合体をポリスチレンの連続相に分散ゴム
粒子となして得られる。
[0008] Rubber-modified polystyrene in the present invention, Poributaji et emissions or butadiene as the butadiene-based polymer - a styrene copolymer was dissolved in styrene monomer, the polymerization solution and eggplant, then stirring heating the polymer solution It is obtained by polymerizing butadiene-based polymer in the form of rubber particles dispersed in a continuous phase of polystyrene.

【0009】重合反応時に溶媒を加えることも出来、そ
の溶剤は芳香族炭化水素類、例えばトルエン、キシレ
ン、エチルベンゼンの単独又は2種以上の混合物が使用
出来る。前記重合液は100〜180℃の温度で重合し
うるが、品質を高めるために重合開始剤が使用される。
A solvent may be added during the polymerization reaction, and the solvent may be an aromatic hydrocarbon, for example, toluene, xylene, ethylbenzene, or a mixture of two or more thereof. The polymerization solution can be polymerized at a temperature of 100 to 180 ° C, and a polymerization initiator is used to improve the quality.

【0010】使用出来る重合開始剤として1,1−ビス
(t−ブチルパーオキシ)シクロヘキサン、1,1−ビ
ス(t−ブチルパーオキシ)3,3,5−トリメチルシ
クロヘキサン等のパーオキシケタール類、ジ−t−プチ
ルパーオキサイド、2,5−ジメチル−2,5−ジ(t
−ブチルパーオキシ)ヘキサン等のジアルキルパーオキ
サイド類、ベンゾイルパーオキサイド、m−トルオイル
パーオキサイド等のジアルパーオキサイド類、ジミリス
チルパーオキシジカーボネート等のパーオキシジカーボ
ネート類、t−ブチルパーオキシイソブロビルカーボネ
ート等のパーオキシエステル類、シクロヘキサノンパー
オキサイド等のケトンパーオキサイド類、p−メンタハ
イドロパーオキサイド等のハイドロパーオキサイド類が
ある。
Peroxy ketals such as 1,1-bis (t-butylperoxy) cyclohexane and 1,1-bis (t-butylperoxy) 3,3,5-trimethylcyclohexane as usable polymerization initiators; Di-t-butyl peroxide, 2,5-dimethyl-2,5-di (t
Dibutyl peroxides such as -butylperoxy) hexane; dialpoxides such as benzoyl peroxide and m-toluoyl peroxide; peroxydicarbonates such as dimyristyl peroxydicarbonate; t-butylperoxyisobromide There are peroxyesters such as bicarbonate, ketone peroxides such as cyclohexanone peroxide, and hydroperoxides such as p-mentha hydroperoxide.

【0011】重合反応は、温度50〜150℃、好まし
くは90〜135℃の範囲で、一定温度あるいは漸次昇
温して行う本発明に特定される、ゴム粒子径が0.0
5〜1.0μmでその粒子径の分布が1.5以下という
均一微細な特殊なゴム粒子は、用いるブタジエン系重合
体のポリスチレンに対する親和性を高める、重合液の粘
度を調整する、撹拌の速度と時間を調整する、均質な撹
拌装置を用いる等多く製造要件によって得られる(例え
ば特開昭60−130613号公報)。
The polymerization reaction is carried out at a temperature of 50 to 150 ° C., preferably 90 to 135 ° C., at a constant temperature or gradually raised . The rubber particle diameter specified in the present invention is 0.0
Uniform and fine special rubber particles having a particle size distribution of 5 to 1.0 μm and a particle size distribution of 1.5 or less increase the affinity of the butadiene-based polymer to polystyrene, adjust the viscosity of the polymerization solution, and stir speed. It can be obtained according to many manufacturing requirements such as adjusting the time and using a homogeneous stirring device (for example, JP-A-60-130613).

【0012】かくの如きゴム粒子の構造は図4,図5に
示すように、ポリブタジエン粒子の内部に単数のポリス
チレン小粒子が内包された、いわゆるコアーシェル構
造、あるいは、図6,図7に示すようにポリブタジエン
粒子の内部に複数のポリスチレン小粒子が内包された、
いわゆるサラミ構造に形成される。上記コアーシェル構
造粒子を有するゴム変性ポリスチレンは、ブタジエン系
重合体としてポリブタジエンブロック1個とポリスチレ
ンブロック1個又は2個よりなる2型又は3型ブロック
共重合体を用いることにより効率よく得ることが出来
る。
As shown in FIGS. 4 and 5, the structure of such rubber particles is a so-called core-shell structure in which a single polystyrene small particle is contained inside polybutadiene particles, or as shown in FIGS. 6 and 7. A plurality of polystyrene small particles are included inside the polybutadiene particles,
It is formed into a so-called salami structure. The rubber-modified polystyrene having the core-shell structured particles can be efficiently obtained by using a type 2 or type 3 block copolymer comprising one polybutadiene block and one or two polystyrene blocks as a butadiene-based polymer.

【0013】又ブロック共重合体中のポリスチレンブロ
ックの含量は20−45重量%の範囲にあることが好ま
しく、このようなブタジエン系重合体の例は、例えば特
開昭64−74208号公報に開示されている。又上記
ゴム粒子の構造は、樹脂組成物の超薄切片法により撮影
した透過型電子顕微鏡写真により確認する事が出来る。
The content of the polystyrene block in the block copolymer is preferably in the range of 20 to 45% by weight. Examples of such a butadiene-based polymer are disclosed in, for example, JP-A-64-74208. Have been. The structure of the rubber particles can be confirmed by a transmission electron micrograph taken by an ultra-thin section method of the resin composition.

【0014】又本発明の発泡成形体を得る方法は次の様
である。ゴム変性ポリスチレン樹脂を連続的に押出機に
供給し、押出機内で加熱溶融しながら押出機のダイに設
けられた細孔より糸状に押出した後、直ちに水を貯えた
冷却バスで冷却しつつ上下2本の駆動ロールで挟み引取
りながら回転式カッターで長さ方向にカットし樹脂粒子
を得る。
The method for obtaining the foamed molded article of the present invention is as follows. The rubber-modified polystyrene resin is continuously supplied to the extruder, extruded into a thread form from the holes provided in the die of the extruder while being heated and melted in the extruder, and immediately cooled up and down by a cooling bath containing water. The resin is cut in the length direction by a rotary cutter while being picked up by two driving rolls to obtain resin particles.

【0015】次に当該樹脂粒子100g量についてイソ
ペンタン,ノルマルペンタン,イソブタン、ノルマルブ
タン,ヘキサン等の揮発性有機発泡剤を0.07〜0.
25グラムモル量含浸して発泡性樹脂粒子を得る。尚揮
発性有機発泡剤を含浸する方法は、例えば、オートクレ
ーブ内に当該樹脂粒子を入れて、これに揮発性有機発泡
剤を加えて満して密閉した後、加温加圧して含浸する方
法又は当該樹脂粒子を押出機内で加圧溶融した後別途押
出機に通じる発泡剤供給ラインを通して揮発性有機発泡
剤を圧入して、溶融状態にある樹脂と十分混合し、その
後押出機のダイ部に設けられた細孔より糸状に押出し、
直に水を貯えた冷却バスで冷却しつつ、上下2本の駆動
ロールで挟み引取りながら回転式カッターで長さ方向に
カットし発泡性樹脂粒子を得る方法が用いられる。
Next, a volatile organic foaming agent such as isopentane, normal pentane, isobutane, normal butane, hexane or the like is used in an amount of 0.07 to 0.
The impregnating resin is impregnated with 25 gmol to obtain foamable resin particles. The method of impregnating the volatile organic foaming agent is, for example, putting the resin particles in an autoclave, adding the volatile organic foaming agent to the resin particles, sealing the container, and then impregnating by heating and pressing or After the resin particles are melted under pressure in an extruder, a volatile organic foaming agent is press-fitted through a foaming agent supply line that is separately connected to the extruder, sufficiently mixed with the resin in a molten state, and then provided in a die portion of the extruder. Extruded into a thread from the pores provided,
A method is used in which foaming resin particles are obtained by cutting in a length direction with a rotary cutter while sandwiching and being taken up by two upper and lower drive rolls while being cooled by a cooling bath storing water directly.

【0016】つぎにこれら発泡性樹脂粒子を公知のポリ
スチレン発泡ビーズ用成形機でスチームによって高発泡
し、目標とする嵩密度が0.009〜0.014g/c
cの発泡粒子となす。当該発泡粒子を用いて本発明の目
標とする性能を備えた独立気泡構造に富んだところの低
密度発泡成形体を得ようとする観点からは、1回で目標
の嵩密度に発泡するいわゆる一段発泡方法にすることが
望ましい。
Next, these expandable resin particles are highly expanded by steam using a known molding machine for polystyrene expanded beads, and the target bulk density is 0.009 to 0.014 g / c.
c to form expanded particles. From the viewpoint of obtaining a low-density foamed molded article having a closed cell structure with the target performance of the present invention using the foamed particles, a so-called one-stage foaming process in which the foam is foamed to a target bulk density in one step It is desirable to use a foaming method.

【0017】その理由は、かならずしも明らかでない
が、数回の発泡によって目標の嵩密に発泡する、いわゆ
る多段発泡方法によれば、高度に低密度なるがゆえに、
極めて薄膜状である発泡粒子の気泡膜が、繰返されるス
チーム加熱によって損傷が大きくなるためと考えられて
いる。この様にして得た発泡樹脂粒子をこれも公知のポ
リスチレン発泡ビーズ用自動成形機で融着1体化して発
泡成形体を得ることが出来る。
Although the reason is not always clear, according to the so-called multi-stage foaming method in which foaming is carried out to a target bulky by foaming several times, since the density is extremely low,
It is considered that the foam film of the foamed particles having a very thin film shape is greatly damaged by repeated steam heating. The foamed resin particles thus obtained can be fused into one body by a known automatic molding machine for polystyrene foam beads to obtain a foam molded body.

【0018】[0018]

【作用】図1は、本発明のゴム変性ポリスチレン樹脂の
ブタジエン成分の占める量の意義を示す実験図である。
即ち図1の横軸は、ブタジエン成分の含量を重量%で示
し、縦軸は〔気泡膜のパンク発生荷重〕と〔低応力緩衝
係数〕の2つの観点からの評価を示す。
FIG. 1 is an experimental view showing the significance of the amount occupied by the butadiene component in the rubber-modified polystyrene resin of the present invention.
That is, the horizontal axis in FIG. 1 shows the content of the butadiene component in% by weight, and the vertical axis shows the evaluation from two viewpoints: [load at which puncturing occurs in the bubble film] and [low stress buffering coefficient].

【0019】即ち、発泡成形体の密度を0.011g/
cm3 に揃えて評価した時に〔気泡膜のパンク発生荷
重〕は、成分量の減少と共に低下しかつブタジエン成分
量が5重量%未満では著しく悪化することが示される。
反面〔低応力緩衝係数〕はブタジエン成分の含量が7.
5重量%付近で最も良好な値を示しさらにブタジエン成
分量が15重量%を越えると著しく悪化することが示さ
れ目標に応じて特性の改善された組成が得られることが
分る。そしてこの様にブタジエン成分量との関係におい
て相反する性質を示す〔気泡膜のパンク発生荷重〕と
〔低応力緩衝係数〕の2つを同時に満足させようとする
観点からは、図1に示す点線の範囲すなわちブタジエン
成分量が5〜15重量%の範囲の組成を選ぶことが望ま
しい。
That is, the density of the foamed molded article is 0.011 g /
When evaluated in conformity with cm 3 , it is shown that the [puncture load of the bubble film] decreases with a decrease in the amount of the component, and remarkably worsens when the butadiene component amount is less than 5% by weight.
On the other hand, the content of the butadiene component is 7.
It shows the best value around 5% by weight, and further shows that the butadiene component content is significantly worse when the amount exceeds 15% by weight. It can be seen that a composition with improved characteristics can be obtained according to the target. From the viewpoint of simultaneously satisfying two factors, that is, the puncture load of the bubble film and the low stress buffering coefficient, which exhibit properties that are contradictory in relation to the butadiene component amount, the dotted line shown in FIG. , That is, a composition in which the butadiene component amount is in the range of 5 to 15% by weight.

【0020】図2は本発明のゴム変性ポリスチレン樹脂
のブタジエン系重合体ゴム粒子の意義を示す実験図であ
る。即ち図2の横軸は、平均ゴム粒子径(μm)を示し
縦軸は〔独立気泡率〕の評価を示す。又図2中の複数の
線図は各々ゴム粒子径の分布を示す。
FIG. 2 is an experimental view showing the significance of butadiene polymer rubber particles of the rubber-modified polystyrene resin of the present invention. That is, the horizontal axis in FIG. 2 shows the average rubber particle diameter (μm), and the vertical axis shows the evaluation of [closed cell rate]. A plurality of diagrams in FIG. 2 each show the distribution of the rubber particle diameter.

【0021】第一に平均ゴム粒子径が大きくなると得ら
れる発泡成形体の独立気泡率は低下し、さらに平均ゴム
粒子径が1.0μmを越えると著しく悪化することが示
される。第二に平均ゴム粒子径が1.0μm未満であっ
てもゴム粒子径分布が1.5の値を越えるとやはり得ら
れる発泡成形体の独立気泡率は著しく低下することが示
されている。即ち得られる発泡成形体の特性を高める観
点から最も重要となる高い独立気泡構造の発泡成形体を
得るためには、重量平均値で表すゴム粒子径が1.0μ
m以下であって、さらに言えば実質工業的に得ることが
可能であるところの0.05〜1.0μmであり、かつ
そのゴム粒子の分布が1.5以下、望ましくば、ゴム粒
子径が0.05〜0.7μmでかつその分布が1.2以
下の範囲であることを示している。
First, it is shown that as the average rubber particle diameter increases, the closed cell ratio of the obtained foamed molded article decreases, and when the average rubber particle diameter exceeds 1.0 μm, it significantly deteriorates. Secondly, even if the average rubber particle diameter is less than 1.0 μm, if the rubber particle diameter distribution exceeds the value of 1.5, it is also shown that the closed cell ratio of the obtained foamed molded article is significantly reduced. That is, in order to obtain a foam having a high closed-cell structure, which is most important from the viewpoint of enhancing the properties of the obtained foam, a rubber particle diameter represented by a weight average value must be 1.0 μm.
m or less, more specifically 0.05 to 1.0 μm, which can be obtained practically industrially, and the distribution of the rubber particles is 1.5 or less, preferably the rubber particle diameter is It shows that the distribution is 0.05 to 0.7 μm and the distribution is 1.2 or less.

【0022】図3は、本発明の発泡成形体の密度の意義
を示す実験図である。即ち図3の横軸は、発泡成形体の
密度(g/cm3 )を示し縦軸は〔低応力緩衝係数〕と
〔圧縮歪の回復量〕の2つの観点からの評価を示す。
FIG. 3 is an experimental view showing the significance of the density of the foam molded article of the present invention. That is, the horizontal axis in FIG. 3 shows the density (g / cm 3 ) of the foamed molded product, and the vertical axis shows the evaluation from two viewpoints of [low stress buffering coefficient] and [compression recovery].

【0023】図3によれば、発泡成形体の密度が大きく
なると共に「圧縮歪の回復量」が低下し、さらに発泡成
形体の密度が0.014g/cm3 を越えると急激に悪
化することが示される。反面〔低応力緩衝係数〕は発泡
成形体の密度が小さくなると悪化し、さらに発泡成形体
の密度が0.009g/cm3 未満では著しく悪化する
事が示され目標に応じて特性の改善された発泡成形体が
得られる事が分る。
According to FIG. 3, as the density of the foamed article increases, the "recovery amount of compression strain" decreases, and when the density of the foamed article exceeds 0.014 g / cm 3 , it rapidly deteriorates. Is shown. On the other hand, the [low stress buffering coefficient] deteriorated when the density of the foamed molded article was reduced, and was significantly deteriorated when the density of the foamed molded article was less than 0.009 g / cm 3 , and the characteristics were improved according to the target. It can be seen that a foam molded article is obtained.

【0024】そしてこの様に、発泡成形体の密度との関
係に於いて相反する性質を示す〔低応力緩衝係数〕と
〔圧縮歪の回復量〕を同時に満足させようとする観点か
らは、図3に示す点線の範囲すなわち発泡成形体の密度
が0.009〜0.014g/cm3 の範囲を選ぶこと
が望ましい。ついで表2は、各々の実験の結果を集約
し、性能の評価結果を総合的にまとめて表示したもので
ある。
As described above, from the viewpoint of simultaneously satisfying [low stress buffering coefficient] and [compression strain recovery amount], which show contradictory properties in relation to the density of the foamed molded article, FIG. It is desirable to select the range of the dotted line shown in FIG. 3, that is, the range of the density of the foam molded article of 0.009 to 0.014 g / cm 3 . Next, Table 2 summarizes the results of the respective experiments and comprehensively summarizes and displays the performance evaluation results.

【0025】すなわち本発明の発泡成形体によれば、全
ての評価項目に於いて劣るという評価は(表中×及び△
印で記載)されるものは見られず優れた性能を示すもの
であることが分る。上記から、用いるゴム変性ポリスチ
レン樹脂のブタジエン成分の含量とそのゴム粒子径その
分布及び得られる発泡成形体の密度と独立気泡率の全て
を特定することで、初めて本発明の目的とする〔低応力
緩衝吸収性能〕と〔圧縮歪の回復性能〕と〔耐気泡のパ
ンク防止性能〕の3つを同時に満足出来る緩衝包装材料
が得られることが分る。
That is, according to the foamed molded article of the present invention, all the evaluation items were evaluated as inferior (× and 中 in the table).
No.) are shown and show excellent performance. From the above, the content of the butadiene component of the rubber-modified polystyrene resin to be used, the distribution of the rubber particle size thereof, and the density and closed cell rate of the obtained foamed molded article are all specified, and the object of the present invention is the first [low stress It can be seen that a buffer wrapping material that can simultaneously satisfy the three requirements of "buffer absorption performance", "compression strain recovery performance", and "bubble resistance puncture prevention performance" can be obtained.

【0026】前述したように、本発明のゴム変性ポリス
チレン樹脂による発泡成形体によれば、高度に低密度化
が達成出来、軽量物の緩衝包装材に必要な「低応力緩衝
性能」に優れ、且つ基本的な緩衝性能である「圧縮歪の
回復性能」と「耐気泡のパンク防止性能」を兼備した軽
量物用の緩衝包装材が得られるという効果が究明され
た。
As described above, according to the foamed molded article of the rubber-modified polystyrene resin of the present invention, a high density can be achieved at a high level, and the "low stress buffering performance" required for a lightweight cushioning packaging material is excellent. In addition, the effect of obtaining a cushioning material for lightweight articles having both the basic cushioning performances of “compression strain recovery performance” and “air bubble resistance puncture prevention performance” was obtained.

【0027】この様な効果が生じる作用機構は、かなら
ずしも明らかで無いが以下の様に考えられている。すな
わち本発明に用いるゴム変性ポリスチレンン樹脂に於い
て、 (イ)発泡成形体を形成する気泡膜の内部に粒子状に分
散し存在するゴム成分が落下衝撃を受けることによって
生じる内部応力を緩和して「パンク現象」といわれる気
泡膜の破壊を効果的に防止していること。
The mechanism of action that produces such an effect is not necessarily clear, but is considered as follows. That is, in the rubber-modified polystyrene resin used in the present invention, (a) a rubber component dispersed and present in the form of particles inside a cell membrane forming a foamed molded article is relieved of internal stress caused by a drop impact. Effectively preventing the destruction of the bubble film, which is referred to as the "puncture phenomenon."

【0028】(ロ)発泡剤を非常に透過して逸散しやす
いゴム成分を、高度に高発泡化されて極めて薄膜状にあ
る気泡膜の厚みよりも十分に小さい値である平均粒子径
で1.0μm以下の粒子状で分散し、存在させることで
気泡膜の厚み方向に対しゴム粒子を充分にポリスチレン
相で覆うことが出来、ポリスチレン樹脂のもつ発泡剤を
逸散しにくい性質を活用出来ていること。
(B) The rubber component which is very permeable to the foaming agent and easily escapes has an average particle diameter which is a value sufficiently smaller than the thickness of the highly foamed and extremely thin foam film. By dispersing in the form of particles having a particle size of 1.0 μm or less, the rubber particles can be sufficiently covered with the polystyrene phase in the thickness direction of the cell membrane, and the property that the foaming agent of the polystyrene resin is not easily dissipated can be utilized. That

【0029】(ハ)ゴム粒子径の分布が大きい事は、極
めて薄い気泡膜の厚み断面の組成,構造等を非常に不均
質にし気泡が膨張して気泡膜が平面方向に伸びて生長し
ようとする時、不均一に生長したり部分的に生長しにく
かったりする現象を誘発し気泡膜が破壊しやすくなるた
めと考えられている。したがって、本発明でいうゴム粒
子径の分布を1.5以下、望ましくは1.2以下の調整
した均一ゴム粒子を用いることが、得られる発泡成形体
の独立気泡構造の形成を高めていると考えられている。
上記の作用機構が相乗的な効果を生んで、本発明の目標
とする性能が得られるものと考えられている。
(C) The large distribution of the rubber particle diameter means that the composition, structure, etc., of the cross section of the extremely thin cell membrane is very inhomogeneous, the cells expand, the cell membrane expands in the plane direction, and tends to grow. It is considered that when this occurs, a phenomenon of non-uniform growth or partial growth difficulty is induced, and the bubble film is easily broken. Accordingly, the use of uniform rubber particles having a distribution of the rubber particle diameter of 1.5 or less, preferably 1.2 or less in the present invention enhances the formation of the closed cell structure of the obtained foamed molded article. It is considered.
It is believed that the mechanism of action described above produces a synergistic effect to achieve the targeted performance of the present invention.

【0030】〔測定方法〕 1)平均粒子径 ゴム変性ポリスチレン樹脂を超薄切片法により撮影した
透過型電子顕微鏡写真中のブタジエンゴム粒子500〜
1000個の粒子径を測定し、次式により算出する。
[Measurement method] 1) Average particle diameter Butadiene rubber particles 500 to 500 in a transmission electron micrograph taken of a rubber-modified polystyrene resin by an ultra-thin section method.
The particle diameter of 1000 particles is measured and calculated by the following equation.

【0031】[0031]

【数1】 (Equation 1)

【0032】[0032]

【数2】 (Equation 2)

【0033】2)粒子径分布 次式により算出する。2) Particle size distribution Calculated by the following equation.

【0034】[0034]

【数3】 (Equation 3)

【0035】3)嵩密度 内容積が1000ccである計量容器によって正確に嵩
容積が1000ccになる様に発泡粒子を秤量する。つ
いで秤量した発泡粒子全量の重量を測定し、次式により
算出する。
3) Bulk density The expanded particles are weighed in a measuring container having an internal volume of 1000 cc so that the bulk volume becomes exactly 1000 cc. Then, the weight of the total amount of the weighed expanded particles is measured and calculated by the following equation.

【0036】[0036]

【数4】 (Equation 4)

【0037】4)密度 重量(Wg)既知の発泡体の容積(Vcm3 )を水没法
で測定し、その重量を容積で除した値を密度(g/cm
3 )とする。
4) Density Weight (Wg) The volume (Vcm 3 ) of a known foam is measured by a submersion method, and the value obtained by dividing the weight by the volume is the density (g / cm).
3 ).

【0038】5)独立気泡率 密度(g/cm3 )が既知の発泡体約24cm3 の真の
容積を東芝・ベックマン社製空気比較式比重計930形
を用いて測定し、次式より独立気泡率〔S,(%)〕を
算出する。
5) Closed cell ratio The true volume of about 24 cm 3 of a foam having a known density (g / cm 3 ) was measured by using an air comparison type hydrometer 930 manufactured by Toshiba Beckman Co., Ltd. The bubble rate [S, (%)] is calculated.

【0039】[0039]

【数5】 (Equation 5)

【0040】6)低応力緩衝係数 JIS−Z−0235に準じ、落下高さ80cm、試験
体の厚み5cm、静的応力値0.03kg/cm2 の条
件で落下衝撃試験を行い、最大加(減)速度を求める、
データは落下回数1回目のものとし、このデータを基に
以下の様に求めた。
6) Low stress buffering coefficient According to JIS-Z-0235, a drop impact test was performed under the conditions of a drop height of 80 cm, a test specimen thickness of 5 cm, and a static stress value of 0.03 kg / cm 2 , Decrease) Find the speed,
The data was the number of times of the first drop, and based on this data, it was determined as follows.

【0041】[0041]

【数6】 (Equation 6)

【0042】7)圧縮歪の回復量 JIS K−6767繰返圧縮永久歪試験法に準じ縦×
横×厚さ寸法が各々50mm×50mm×50mmの試
験体を25%圧縮試験を行い以下の様に求めた。
7) Amount of recovery of compressive strain Vertical X according to JIS K-6767 repeated compression set test method
Specimens each measuring 50 mm × 50 mm × 50 mm in width × thickness were subjected to a 25% compression test and determined as follows.

【0043】[0043]

【数7】R :圧縮永久歪の回復量(mm) R1 :25%圧縮時の厚み寸法(mm) R2 :回復後の厚み寸法(mm) R=R2 −R1
Equation 7] R: recovered amount of compression set (mm) R 1: 25% -compression of the thickness (mm) R 2: thickness after recovery (mm) R = R 2 -R 1
.

【0044】8)気泡のパンク発生重量 JIS−Z−0235、落下衝撃試験法に準じ縦×横×
厚さ寸法が各々100mm×100mm×50mmの試
験体の縦×横の上面の全面に上面から80cmの高さか
ら重量が50g単位で異る平板状の錘りを順次落下し衝
撃と圧縮歪を与え試験体である発泡成形体の気泡膜に破
裂が生じ初める時の錘りの重量を求め、気泡のパンク発
生重量とする。尚一度落下衝撃試験を行った試験体は再
び使用せず新しい試験体に交換し次の落下衝撃試験を行
うものとする。
8) Weight of puncture of air bubbles Vertical × horizontal × according to JIS-Z-0235, drop impact test method
A flat weight having a weight of 50 g is dropped from a height of 80 cm from the upper surface on the entire upper surface of the test specimen having a thickness of 100 mm x 100 mm x 50 mm from the upper surface to the lower surface in order to reduce impact and compressive strain. The weight of the weight when bursting starts to occur in the foam film of the foamed molded article as the test specimen is determined, and is defined as the weight of punctured bubbles. It should be noted that the test specimen once subjected to the drop impact test shall be replaced with a new test specimen without using again, and the next drop impact test shall be performed.

【0045】〔評価方法〕 (1)低応力衝撃吸収性能 前記低応力緩衝係数の項で求めた値によって以下の評価
尺度で求める。
[Evaluation method] (1) Low stress impact absorption performance The low stress shock absorption coefficient is determined by the following evaluation scale based on the value determined in the section of the low stress buffer coefficient.

【0046】[0046]

【表1】 [Table 1]

【0047】(2)圧縮歪の回復性能 前記圧縮歪の回復量の測定方法の項で求めた圧縮歪の回
復量(mm)の値によって、以下の評価尺度で求めた。
(2) Compressive strain recovery performance The following evaluation scale was used to determine the amount of compressive strain recovery (mm) obtained in the section on the method of measuring the amount of recovery of compressive strain.

【0048】[0048]

【表2】 [Table 2]

【0049】(3)耐気泡のパンク防止性能 前記気泡のパンク発生重量の測定方法の項で求めた気泡
のパンク発生重量(kg)の値によって以下の評価尺度
で求めた。
(3) Puncture Prevention Performance of Air Bubble Resistance The puncture generation weight (kg) of the bubble obtained in the section of the method of measuring the puncture generation weight of the bubble was determined by the following evaluation scale.

【0050】[0050]

【表3】 [Table 3]

【0051】[0051]

【表4】 [Table 4]

【0052】[0052]

【実施例】以下本発明の内容を実施例を用いて詳述す
る。 〔ゴム変性ポリスチレンの調整〕表5,6,7に示すと
ころの配合比でスチレンモノマーにブタジエン系重合体
を溶解し、溶解した溶液100部にエチルベンゼン5
部、1,1−ビス(t−ブチルパーオキシ)シクロヘキ
サン0.05部を添加し重合原料液を調整する。各々の
原料液を各々別に連続3段式重合器に送入し重合を行っ
た。各重合機は、1.2リットルの容積を有し撹拌翼が
付いている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The contents of the present invention will be described below in detail with reference to embodiments. [Adjustment of Rubber-Modified Polystyrene] A butadiene-based polymer was dissolved in a styrene monomer at a compounding ratio shown in Tables 5, 6, and 7, and ethylbenzene 5 was added to 100 parts of the dissolved solution.
And 1,1-bis (t-butylperoxy) cyclohexane are added to adjust the polymerization raw material liquid. Each of the raw material liquids was separately fed into a continuous three-stage polymerization vessel to perform polymerization. Each polymerizer has a volume of 1.2 liters and is equipped with stirring blades.

【0053】重合温度は105〜145℃の間で変化さ
せ、最終重合器出で固型分が約80%となるまで重合さ
せた後、加熱真空下の脱揮装置に送り未反応スチレンモ
ノマー及びエチルベンゼンを除去し、ダイスからストラ
ンドを引き水冷後ペレット状に切断する。ペレット中の
ブタジエン成分の含有量を測定後、必要であればポリス
チレン樹脂(旭化成工業社製スタイロン683)にて3
0mmφ単軸押出機を用いて希釈し表5,6,7に示す
ところの各々のブタジエン成分量に調整した。又重合の
過程で、重合の温度条件,撹拌の条件等を調整し、最終
的に表5、6,7に示すところのゴム変性ポリスチレン
樹脂(HIPS1〜20)を得た。
The polymerization temperature was varied between 105 ° C. and 145 ° C., and was polymerized to a solid content of about 80% in the final polymerization reactor. Ethylbenzene is removed, the strand is drawn from the die, cooled with water, and cut into pellets. After measuring the content of the butadiene component in the pellet, if necessary, use a polystyrene resin (Stylon 683, manufactured by Asahi Kasei Kogyo Co., Ltd.).
It was diluted using a 0 mmφ single screw extruder and adjusted to the respective butadiene component amounts shown in Tables 5, 6, and 7. In the course of the polymerization, the temperature conditions of the polymerization, the conditions of the stirring, and the like were adjusted to finally obtain rubber-modified polystyrene resins (HIPS 1 to 20) shown in Tables 5, 6, and 7.

【0054】実施例、比較例1 上記ゴム変性ポリスチレン樹脂を各々別に発泡剤の加圧
供給装置をもち、かつその加圧供給装置からの接続ライ
ンが押出機のシリンダー内の溶融混練部に通じるように
連結され、さらに前頭部に樹脂の冷却装置と多数の樹脂
への流出孔をもつダイ装置を備えた押出含浸装置に供給
し、押出機内で溶融混練しつつ、発泡剤の加圧供給装置
からイソペンタンを樹脂100g量について0.15グ
ラムモル量の比率にポンプで一定量づつ加圧供給し、樹
脂と混練混合しつつ冷却装置で適温に冷却しダイ装置に
設けられた多数の細孔より糸状に押出して、直ちに冷却
水を貯えた冷却バスを介して引取りながら回転式カッタ
ーで長さ方向にカットし、各々の発泡性樹脂粒子を得
た。
Examples and Comparative Example 1 Each of the above rubber-modified polystyrene resins was separately provided with a pressure-supplying device for a foaming agent, and a connection line from the pressure-supplying device was connected to a melt-kneading section in a cylinder of an extruder. To the extrusion impregnating device, which is equipped with a resin cooling device and a die device having a large number of outlet holes for the resin in the forehead, and pressurizes and supplies the foaming agent while melting and kneading in the extruder. Is pumped at a constant rate of 0.15 gram mole per 100 g of resin, and cooled to an appropriate temperature with a cooling device while kneading and mixing with the resin. And immediately cut in the length direction with a rotary cutter while taking it through a cooling bath storing cooling water to obtain each expandable resin particle.

【0055】実験例1 ゴム変性ポリスチレン、HIPS−1より前述の方法で
得た発泡性樹脂粒子をスチーム発泡機で、いわゆる1段
発泡法といわれる1回の発泡で嵩密度が目標であるとこ
ろの0.011g/cm3 の発泡樹脂粒子を得た。つい
でこの発泡樹脂粒子を20℃の室内で24時間熟成した
後、発泡スチロール用成形機(笠原工業社製;PION
Y−75型)で成形し厚さ,長さ,巾の各々の寸法が5
0mm×300mm×300mmの板状発泡樹脂成形体
を得た。次にこの板状発泡樹脂成形体を湿度が50℃の
乾燥室で3時間乾燥後取出しさらに20℃の室内で24
時間熟成した後、嵩密度を測定したところ0.011g
/cm3であることを確認して評価した結果を表8、表
9に示す。
EXPERIMENTAL EXAMPLE 1 Expandable resin particles obtained from rubber-modified polystyrene and HIPS-1 by the above-mentioned method were subjected to a single-stage expansion method called a one-stage expansion method using a steam expander to achieve a target bulk density. 0.011 g / cm 3 of foamed resin particles were obtained. Then, after the foamed resin particles are aged in a room at 20 ° C. for 24 hours, a molding machine for styrene foam (manufactured by Kasahara Kogyo; PION)
(Y-75 type) and each thickness, length and width are 5
A 0 mm × 300 mm × 300 mm plate-like foamed resin molded product was obtained. Next, the plate-like foamed resin molded product was dried in a drying room at a humidity of 50 ° C. for 3 hours and then taken out.
After aging for 0.01 hour, the bulk density was measured to be 0.011 g
/ Cm 3 and the results of evaluation are shown in Tables 8 and 9.

【0056】実験例2〜22 表8,表9に示す実験番号に対応するところのゴム変性
ポリスチレン樹脂(表5、6、7に詳述している)によ
り各々実験例1と同様の方法で得た発泡性樹脂粒子を、
やはり実験例1と同様に発泡し成形して実験番号に対応
する発泡成形体を得て評価した結果をまとめて表8、表
9に表す。
EXPERIMENTAL EXAMPLES 2 to 22 Rubber-modified polystyrene resins corresponding to the experimental numbers shown in Tables 8 and 9 (described in detail in Tables 5, 6, and 7) were used in the same manner as in Experimental Example 1. The obtained expandable resin particles,
Similarly, the foaming and molding were performed in the same manner as in Experimental Example 1 to obtain a foamed molded product corresponding to the experiment number, and the evaluation results are shown in Tables 8 and 9.

【0057】比較例2 前記の方法で得たゴム変性ポリスチレン、HIPS−2
に、イソペンタンを樹脂100g量について0.05グ
ラムモル量の比率にポンプで一定量づつ加圧供給したこ
とを変えた意外は全く実施例1と同様の方法で発泡性樹
脂粒子を得た。ついでこの発泡樹脂をスチーム発泡機で
発泡し嵩密度が0.033g/ccの発泡樹脂粒子を得
た。つぎに当該発泡樹脂粒子を室内に24時間放置し熟
成後再び前記スチーム発泡機で発泡し目標の嵩密度が
0.011g/ccの発泡樹脂粒子を得て20℃の室内
で24時間熟成した後、実験例1と同様に成形してその
密度が0.011g/cm3 の発泡成形体を得て評価し
た結果を表8、表9に示す。
Comparative Example 2 Rubber-modified polystyrene obtained by the above method, HIPS-2
In addition, foaming resin particles were obtained in exactly the same manner as in Example 1, except that isopentane was supplied under a constant pressure by a pump at a ratio of 0.05 gram mole per 100 g of resin. Then, the foamed resin was foamed with a steam foaming machine to obtain foamed resin particles having a bulk density of 0.033 g / cc. Next, the foamed resin particles are allowed to stand in a room for 24 hours, and after aging, are foamed again by the steam foaming machine to obtain foamed resin particles having a target bulk density of 0.011 g / cc and are aged in a room at 20 ° C. for 24 hours. Tables 8 and 9 show the results of evaluation obtained by molding a foamed article having a density of 0.011 g / cm 3 by molding in the same manner as in Experimental Example 1.

【0058】[0058]

【表5】 [Table 5]

【0059】[0059]

【表6】 [Table 6]

【0060】[0060]

【表7】 [Table 7]

【0061】[0061]

【表8】 [Table 8]

【0062】[0062]

【表9】 [Table 9]

【0063】[0063]

【発明の効果】以上詳述して明らかにしてきた通り、本
発明の低密度発泡樹脂成形体は、上述の構成をもつこと
により、衝撃吸収性能、圧縮歪の回復性能、耐衝撃破壊
性能を兼備し、緩衝包装用途に優れた発泡成形体という
利点があり、例えば電子部品、音響機器又は通信機器等
の軽量で破損しやすい内容物の緩衝包装に用いることが
出来かつ、低密度なるがゆえに使用重量を削減し産業廃
棄物の発生量を大巾に低減出来る産業界に果す役割の高
い優れた発明である。
As has been described in detail above, the low-density foamed resin molded article of the present invention has the above-described structure, and thus has an impact absorption performance, a compression strain recovery performance, and an impact fracture resistance. Combined, has the advantage of excellent foam molded article for buffer packaging applications, for example, can be used for buffer packaging of lightweight and easily breakable contents such as electronic components, audio equipment or communication equipment, and because of low density It is an excellent invention that plays a major role in the industry where the weight used can be reduced and the amount of industrial waste generated can be significantly reduced.

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

【図1】本発明のゴム変性ポリスチレン樹脂のブタジエ
ン成分の占める量の意義を示す実験図
FIG. 1 is an experimental diagram showing the significance of the amount occupied by a butadiene component in a rubber-modified polystyrene resin of the present invention.

【図2】本発明のゴム変性ポリスチレン樹脂のブタジエ
ン系重合体ゴム粒子の意義を示す実験図
FIG. 2 is an experimental diagram showing the significance of butadiene-based polymer rubber particles of the rubber-modified polystyrene resin of the present invention.

【図3】本発明の発泡成形体の密度の意義を示す実験図FIG. 3 is an experimental view showing the significance of the density of the foam molded article of the present invention.

【図4】本発明のゴム変性ポリスチレン樹脂のゴム粒子
の断面を拡大した写生図
FIG. 4 is a sketch drawing in which a cross section of a rubber particle of the rubber-modified polystyrene resin of the present invention is enlarged.

【図5】本発明のゴム変性ポリスチレン樹脂のゴム粒子
の分散状態を示す断面拡大写生図
FIG. 5 is an enlarged cross-sectional sketch showing a dispersion state of rubber particles of the rubber-modified polystyrene resin of the present invention.

【図6】比較品のゴム粒子の断面を拡大した写生図FIG. 6 is a sketch drawing in which a cross section of a rubber particle of a comparative product is enlarged.

【図7】比較品のゴム粒子の分散状態を示す断面拡大写
生図
FIG. 7 is an enlarged cross-sectional sketch showing a dispersion state of rubber particles of a comparative product.

【符号の説明】[Explanation of symbols]

図1の1 緩衝係数 図1の2 衝撃破壊発生荷重 図2の1 粒子径分布が1.2 図2の2 粒子径分布が1.5 図2の3 粒子径分布が2 図3の1 低応力緩衝係数 図3の2 圧縮歪の回復量 図4の1 ポリブタジエン 図4の2 ポリスチレン 図6の1 ポリブタジエン 図6の2 ポリスチレン 1 of FIG. 1 Buffer coefficient FIG. 2 of FIG. 2 Impact fracture initiation load 1 of FIG. 2 Particle size distribution of 1.2 FIG. 2 2 Particle size distribution of 1.5 FIG. Stress buffering coefficient Fig. 3-2 Recovery of compressive strain Fig. 4 1 polybutadiene Fig. 4 2 polystyrene Fig. 6 1 polybutadiene Fig. 6 2 polystyrene

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C08J 9/00 - 9/42 B29C 44/00 ──────────────────────────────────────────────────続 き Continuation of front page (58) Field surveyed (Int. Cl. 7 , DB name) C08J 9/00-9/42 B29C 44/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ポリスチレンの連続相に、内部にポリス
チレンが小粒子状に内包されたブタジエン系重合体ゴム
が粒子状に分散しており、全体に占めるブタジエン成分
の含有量が5〜15重量%であり、かつブタジエン系重
合体ゴム粒子の重量平均粒子径が0.05〜1.0μ
m、その粒子径分布が1.5以下であるゴム変性ポリス
チレン樹脂の発泡粒子からなる成形体であって、その密
度が0.009〜0.014g/cm3 であり、かつそ
の気泡の80%以上が独立気泡構造を有するポリスチレ
ン系樹脂発泡粒子の低密度融着発泡樹脂成形体。
1. A polystyrene continuous phase in which a butadiene polymer rubber in which polystyrene is encapsulated in small particles is dispersed in the form of particles, and the content of the butadiene component in the whole is 5 to 15% by weight. And the weight average particle diameter of the butadiene polymer rubber particles is 0.05 to 1.0 μm.
m, a molded article comprising foamed particles of a rubber-modified polystyrene resin having a particle size distribution of 1.5 or less, having a density of 0.009 to 0.014 g / cm 3 and 80% of the cells The above is a low-density fused foamed resin molded article of polystyrene resin foamed particles having a closed cell structure.
【請求項2】 ポリスチレンの連続相に内部にポリスチ
レンが小粒子状に内包されたブタジエン系重合体ゴムが
粒子状に分散しており、全体に占めるブタジエン成分の
含有量が5〜15重量%であり、かつブタジエン系重合
体ゴム粒子の重量平均粒子径が0.05〜1.0μmで
その粒子径分布が1.5以下であるゴム変性ポリスチレ
ン樹脂100グラム量について揮発性有機発泡剤を0.
07〜0.25グラムモル量を含浸し発泡性樹脂粒子を
得て後、該発泡性樹脂粒子を発泡機内でスチームによっ
て発泡し1回の発泡で嵩密度が0.009〜0.014
g/ccの発泡粒子を得、ついで該発泡粒子を成形型に
導入しスチームで加熱し発泡粒子相互を融着成形してそ
の密度が0.009〜0.014g/cm3 で、かつそ
の気泡の80%以上が独立気泡構造を有するポリスチレ
ン系樹脂発泡粒子の低密度融着発泡樹脂成形体の製造方
法。
2. A butadiene polymer rubber in which polystyrene is encapsulated in small particles in a continuous phase of polystyrene is dispersed in the form of particles, and the content of the butadiene component in the whole is 5 to 15% by weight. The volatile organic blowing agent is added in an amount of 100 grams of a rubber-modified polystyrene resin having a butadiene-based polymer rubber particle having a weight average particle size of 0.05 to 1.0 μm and a particle size distribution of 1.5 or less.
After obtaining foamable resin particles by impregnating the foamable resin particles in an amount of 07 to 0.25 gmol, the foamable resin particles are foamed by steam in a foaming machine, and the bulk density is 0.009 to 0.014 by one foaming.
The resulting foamed particles of g / cc, then the density fused molded foamed particles each other and heated with steam introduced expanded beads in the mold is in 0.009~0.014g / cm 3, and the bubbles A method for producing a low-density fused foamed resin molded article of expanded polystyrene resin particles in which 80% or more of the polystyrene-based resin has a closed cell structure.
JP30833891A 1991-10-29 1991-10-29 Low-density fused expanded resin molded article of polystyrene resin expanded particles and method for producing the same Expired - Fee Related JP3221019B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30833891A JP3221019B2 (en) 1991-10-29 1991-10-29 Low-density fused expanded resin molded article of polystyrene resin expanded particles and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30833891A JP3221019B2 (en) 1991-10-29 1991-10-29 Low-density fused expanded resin molded article of polystyrene resin expanded particles and method for producing the same

Publications (2)

Publication Number Publication Date
JPH05116227A JPH05116227A (en) 1993-05-14
JP3221019B2 true JP3221019B2 (en) 2001-10-22

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0649262A (en) * 1992-07-27 1994-02-22 Sekisui Plastics Co Ltd Expandable styrene resin bead
CN1038843C (en) * 1993-04-27 1998-06-24 旭化成工业株式会社 Expanded foamed bead of a rubber-modified styrene polymer
EP0960904B1 (en) * 1996-12-26 2005-03-09 Kaneka Corporation Expandable polystyrene resin beads, process for the preparation of them, and foam made by using the same
JP3653393B2 (en) 1997-09-12 2005-05-25 株式会社ジェイエスピー Expandable rubber-modified styrenic resin composition
KR20000072536A (en) * 2000-09-08 2000-12-05 정갑철 Manufacturing Method of Soft EPS Boards using Floor Impact Sound Insulation Materials in Apartment Houses
DE10358805A1 (en) * 2003-12-12 2005-07-14 Basf Ag Particle foam moldings made of expandable, impact-modified, thermoplastic polymer granules
JP7156283B2 (en) * 2017-07-19 2022-10-19 日本ゼオン株式会社 How to make foam rubber

Also Published As

Publication number Publication date
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