JPH03182529A - Expandable resin composition and expanded molding thereof - Google Patents

Expandable resin composition and expanded molding thereof

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Publication number
JPH03182529A
JPH03182529A JP32056789A JP32056789A JPH03182529A JP H03182529 A JPH03182529 A JP H03182529A JP 32056789 A JP32056789 A JP 32056789A JP 32056789 A JP32056789 A JP 32056789A JP H03182529 A JPH03182529 A JP H03182529A
Authority
JP
Japan
Prior art keywords
resin
amount
resin composition
conjugated diene
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.)
Granted
Application number
JP32056789A
Other languages
Japanese (ja)
Other versions
JP2841303B2 (en
Inventor
Isao Koba
木葉 勲
Manabu Tanuma
田沼 学
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 Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
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Application filed by Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP1320567A priority Critical patent/JP2841303B2/en
Publication of JPH03182529A publication Critical patent/JPH03182529A/en
Application granted granted Critical
Publication of JP2841303B2 publication Critical patent/JP2841303B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain an expandable resin composition which can show good retentivity of a blowing agent in the production of a foam and can easily give a highly expanded molding by mixing a copolymer resin obtained by hydrogenating a block copolymer of a vinylaromatic compound with a conjugated diene with a high-impact polystyrene resin. CONSTITUTION:An expandable resin composition formed by mixing a copolymer resin which is a block copolymer of a vinylaromatic compound with a conjugated diene compound wherein most of the double bonds derived from the conjugated diene are hydrogenated with a high-impact polystyrene resin. A preferred composition is one having a total rubber component of 10-25wt.% based on the total resin. A preferred high-impact polystyrene resin is one having a rubber component content of 3-15wt.%, though it is not particularly limited. The above copolymer resin is preferably one which has a vinylaromatic compound content of 20-80wt.% and a degree of saturation of the double bonds derived from the conjugated diene >=80%.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、発泡用途、特に型内発泡成形に有用な樹脂組
成物、及びその組成物から出来た発泡体、3゜ 特に緩衝包装用途に有用な発泡成形体に関する。
Detailed Description of the Invention [Field of Industrial Application] The present invention provides a resin composition useful for foaming applications, particularly in-mold foam molding, and a foam made from the composition, particularly for use in cushioning packaging. This invention relates to a useful foam molded article.

〔従来の技術〕[Conventional technology]

従来よりポリスチレン発泡ビーズを成形して得た成形体
は割れ易いことは広く知られている。そしてスチレン発
泡ビーズ成形体のもつ割れ易さ及び圧縮歪の回復性の悪
さを改善しようとする試みがいくつか提案されている。
It is widely known that molded objects obtained by molding polystyrene foam beads are easily broken. Several attempts have been made to improve the breakability and poor compressive strain recovery properties of styrene foam bead moldings.

例えば(1)−船釣には、ポリスチレン樹脂に耐割れ性
に富むポリエチレン樹脂やブタジェンゴムを加え機械的
な方法で混合し発泡用樹脂組成物を得る方法、(2)特
公昭51−46536号公報、特開昭55−52331
号公報には、ハイインパクトポリスチレン樹脂(以下、
HIPS樹脂と称す)により発泡用樹脂組成物を得る方
法、(3)特開昭54−154471号公報、特開昭5
4−158467号公報にはポリスチレン樹脂又はHI
PS樹脂と、スチレンとブタジェンのブロック共重合体
樹脂(以下、SB樹脂と称す)を機械的な方法で混合し
発泡用樹脂組成物を得る方法、(4)特開昭54−11
9563号公報、特開昭57−1.11330号公報に
は、ポリエチレン樹脂又はエチレンと酢酸ビニルの共重
合体樹脂(以下、EVA樹脂と称す)とポリスチレンと
のグラフト重合体樹脂により発泡用樹脂組成物を得る方
法が記述されている。
For example, (1) - for boat fishing, a method of adding crack-resistant polyethylene resin or butadiene rubber to polystyrene resin and mixing by a mechanical method to obtain a foaming resin composition, (2) Japanese Patent Publication No. 51-46536 , Japanese Patent Publication No. 55-52331
In the publication, high impact polystyrene resin (hereinafter referred to as
(3) JP-A-54-154471, JP-A-Sho 5
No. 4-158467 discloses polystyrene resin or HI
Method for obtaining a foaming resin composition by mechanically mixing a PS resin and a block copolymer resin of styrene and butadiene (hereinafter referred to as SB resin), (4) JP-A-11-1989
No. 9563 and Japanese Unexamined Patent Publication No. 57-1.11330 disclose a resin composition for foaming using a graft polymer resin of polyethylene resin or a copolymer resin of ethylene and vinyl acetate (hereinafter referred to as EVA resin) and polystyrene. It describes how to obtain things.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかしながら、上記(1)のポリスチレン樹脂にポリエ
チレン樹脂やブタジェンゴム等の耐割れ性に富む樹脂等
を混合して発泡用樹脂組成物を得る方法においては、加
える樹脂がポリスチレン樹脂と熱的性質が異ること、又
混合性が悪く均質な混合組成物を得ることが出来ない結
果、この発泡用樹脂組成物に後述の方法で揮発性有機発
泡剤を含浸し発泡性樹脂組成物とした時に、極めて高発
泡性に劣り緩衝包装材料に必要な高い倍率の発泡成形体
が得られないという問題があった。また、上記(2)の
HIPS樹脂により発泡用樹脂組成物を得る方法におい
ては、−級にHIPS樹脂は単独で高い耐割れ性を示す
ことが知られているが、このHIPS樹脂から後述の方
法で得た発泡成形体はかならずしもHIPS樹脂単独で
見られるような高い耐割れ性は得られず到底満足出来る
ものでなかった。
However, in the above method (1) of mixing polystyrene resin with resin with high crack resistance such as polyethylene resin or butadiene rubber to obtain a foaming resin composition, the resin to be added has different thermal properties from the polystyrene resin. In addition, as a result of the poor mixability and the inability to obtain a homogeneous mixed composition, when this foaming resin composition is impregnated with a volatile organic blowing agent by the method described below to form a foamable resin composition, it has an extremely high There was a problem in that the foamability was poor and a foamed molded product with a high magnification required for a cushioning packaging material could not be obtained. In addition, in the method (2) above for obtaining a foaming resin composition using a HIPS resin, it is known that HIPS resin alone exhibits high cracking resistance in the - grade. The foamed molded product obtained in the above was not completely satisfactory as it did not necessarily have the high cracking resistance that can be seen with HIPS resin alone.

又、He’s樹脂中樹脂入成分の量と耐割れ性の関係に
おいて、ゴム成分量の増加が、耐割れ性を高めることが
良く知られているが、HIPS樹脂はその製法上の理由
から一般的に加えうるブタジェン量は、全HIPS樹脂
に対し最大量でもほぼ15重量パーセントが限界であり
、この様な理由からも耐割れ性の改善に限界があった。
In addition, regarding the relationship between the amount of resin components in He's resin and cracking resistance, it is well known that increasing the amount of rubber components improves cracking resistance, but HIPS resin has a Generally, the maximum amount of butadiene that can be added is approximately 15% by weight based on the total HIPS resin, and for this reason as well, there is a limit to the improvement in cracking resistance.

さらに、上記(3)のHIPS樹脂にさらに耐割れ性に
富むSB樹脂を機械的な方法で混合する方法においては
、加えるSB樹脂自体の剛性が極めて低い結果、耐割れ
性と圧縮強度特性を同時に満足することが出来ないとい
う問題があった。さらにまた、上記(4)のポリエチレ
ン樹脂又はEVA樹脂とポリスチレンのグラフト重合体
樹脂による発泡用樹脂組成物を得ようとする方法におい
ては、得られる発泡成形体の耐割れ性を必要とする目標
レベルに高めようとすると、ポリエチレン樹脂及びEV
A樹脂等のオレフィン成分量を全樹脂量に対し少なくと
も30重量パーセントを越える高い比率にする必要があ
り、この発泡用樹脂組成物に後述の方法で揮発性有機発
泡剤を含浸し発泡性樹脂組成物を得、これを後述の方法
で発泡粒子を得た時に極めて発泡剤の保持性が低く品質
の安定した発泡成形品が得られにくいこと、又機械的強
度特性の低いオレフィン成分量の割合が高いため得られ
る発泡成形体の圧縮強度特性が低いという問題があった
Furthermore, in the method of (3) above, in which HIPS resin is mechanically mixed with SB resin, which has higher cracking resistance, the rigidity of the added SB resin itself is extremely low. The problem was that I couldn't be satisfied. Furthermore, in the method for obtaining a foaming resin composition using a graft polymer resin of polyethylene resin or EVA resin and polystyrene as described in (4) above, the cracking resistance of the resulting foamed molded product is required to be at a target level. If you try to increase it, polyethylene resin and EV
It is necessary to make the amount of olefin components such as resin A at a high ratio of at least 30% by weight to the total resin amount, and this foaming resin composition is impregnated with a volatile organic blowing agent by the method described below to create a foamable resin composition. When foamed particles are obtained using the method described below, the retention of the blowing agent is extremely low, making it difficult to obtain a foamed molded product with stable quality, and the proportion of the olefin component, which has low mechanical strength properties, is There was a problem that the compressive strength properties of the obtained foamed molded product were low because of the high content.

しかして本発明は上記欠点のすべてを解決しようとする
もので、本発明の目的は発泡体にしようとするときに発
泡剤の保持性に優れ且つ高発泡性に富む発泡成形体にし
易い樹脂組成物を提供することであり、更に発泡成形体
になった時は、圧縮強度、耐割れ性ミ圧縮歪回復性が兼
備された緩衝包装用用途に優れた発泡体を提供すること
である。
Therefore, the present invention is intended to solve all of the above-mentioned drawbacks, and the purpose of the present invention is to create a resin composition that has excellent foaming agent retention properties and is easy to form into a foam molded product with high foamability. The purpose of the present invention is to provide a foamed product having excellent compressive strength, cracking resistance, and compressive strain recovery properties when used as a foamed product for use in shock-absorbing packaging.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は、ビニル芳香族化合物と共役ジエン化合物との
ブロック共重合体であって、共役ジエンに由来する2重
結合の大部分が水素添加され飽和された共重合樹脂(以
下、H3B樹脂と称す)とHIPS樹脂とを混合してな
る発泡用樹脂組成物及びHIPS樹脂とH3B樹脂との
混合樹脂組成物でできた発泡粒子の多数個をその表層部
で融着一体化させて成る発泡成形体である。
The present invention is a block copolymer of a vinyl aromatic compound and a conjugated diene compound, in which most of the double bonds derived from the conjugated diene are hydrogenated and saturated (hereinafter referred to as H3B resin). ) and a HIPS resin, and a foamed molded product made by fusing and integrating a large number of foam particles made of a mixed resin composition of a HIPS resin and an H3B resin at the surface layer thereof. It is.

以下、本発明を図面等を用いて詳述する。Hereinafter, the present invention will be explained in detail using drawings and the like.

本発明の主要とする処はHIPS樹脂とH3B樹脂を混
合して用いることにある。
The main point of the present invention is to use a mixture of HIPS resin and H3B resin.

〔作 用〕[For production]

第1図は本発明の樹脂組成物を用いることの意義を端的
に示す実験図である。即ち、第1図の横軸は全樹脂量に
対する総ゴム成分の占める量を重量パーセントで示すも
のである。この意味は、各々ゴム成分を含むHIPS樹
脂とHSB樹脂の混合において、総ゴム量をもって混合
比を代表して示すものである。
FIG. 1 is an experimental diagram clearly showing the significance of using the resin composition of the present invention. That is, the horizontal axis in FIG. 1 indicates the amount of the total rubber component relative to the total resin amount in weight percent. This meaning is that in mixing HIPS resin and HSB resin, each of which contains a rubber component, the total rubber amount represents the mixing ratio.

縦軸は、〔発泡剤保持時間〕、〔圧縮歪の回復量〕、〔
圧縮強度〕の3つの観点からの評価を示す。すなわち、
第1図によれば、〔圧縮強度〕及び〔発泡剤保持時間〕
は、総ゴム成分量の増加と共に低下しかつ総ゴム成分量
が25重量バーセントを越えると著しく悪化することが
示される。しかし〔圧縮歪の回復量〕は、前記2項とは
相反し総ゴム底分量の低減と共に低下し、さらに総ゴム
成分量が10重量パーセント未満では、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。そしてこの様に総ゴム成分量との関係
において相反する性質を示す〔圧縮強度〕及び〔発泡剤
保持時間〕と〔圧縮歪の回復量〕の3つを同時に満足さ
せようとする観点からは、第1図に示す点線の範囲すな
わち総ゴム成分量が10〜25重量パーセントの範囲の
組成のものを選ぶことが望ましい。
The vertical axis is [foaming agent retention time], [compressive strain recovery amount], [
Evaluation from three viewpoints of compressive strength] is shown below. That is,
According to Figure 1, [compressive strength] and [blowing agent retention time]
It is shown that the ratio decreases as the total amount of rubber components increases, and becomes significantly worse when the total amount of rubber components exceeds 25% by weight. However, it has been shown that [compressive strain recovery amount] decreases as the total rubber bottom content decreases, contrary to the above two items, and further deteriorates significantly when the total rubber content is less than 10% by weight. It can be seen that a composition with improved properties can be obtained. From the point of view of trying to simultaneously satisfy the three properties of [compressive strength], [foaming agent retention time], and [compressive strain recovery], which show contradictory properties in relation to the total rubber component amount, It is desirable to select a composition within the range of the dotted line shown in FIG. 1, that is, the total amount of rubber components in the range of 10 to 25 weight percent.

第2図は本発明の樹脂組成物中の総ゴム成分中のH3B
樹脂のゴム成分の占める量の意義を示す実験図である。
Figure 2 shows H3B in the total rubber component in the resin composition of the present invention.
It is an experimental diagram showing the significance of the amount occupied by the rubber component of the resin.

即ち、第2図の横軸は、総ゴム成分量に対するHSB樹
脂のゴム成分の占める量を重量パーセントで示し、縦軸
は〔割れ量〕、〔発泡倍率〕の2つの観点からの評価を
示す。この第2図によれば全ゴム量に占めるH3B樹脂
のゴム量の減少と共に〔発泡倍率〕は改善され、特にH
3B樹脂のゴム成分量が10重量パーセント以下になる
と著しく改質されることが示される。一方、〔割れ量〕
は、前記〔発泡倍率〕に反しH3B樹脂のゴム成分量の
減少と共に大きく悪化し、特にH3B樹脂のゴム成分量
が10重量パーセント未満では極めて大きな値となり悪
化することが示される。
That is, the horizontal axis in Fig. 2 shows the amount of the rubber component of the HSB resin relative to the total rubber component amount in weight percent, and the vertical axis shows the evaluation from two viewpoints: [cracking amount] and [expansion ratio]. . According to this Figure 2, as the rubber amount of H3B resin in the total rubber amount decreases, the [foaming ratio] improves, especially H3B resin.
It is shown that when the amount of rubber component in the 3B resin is less than 10% by weight, it is significantly modified. On the other hand, [amount of cracking]
Contrary to the above-mentioned [expansion ratio], the ratio deteriorates significantly as the amount of rubber component of the H3B resin decreases, and in particular, when the amount of rubber component of the H3B resin is less than 10% by weight, it becomes an extremely large value and deteriorates.

即ち、目標に応じた改善点を組成申の全体ゴム成分量に
占めるH3Bのゴム成分量の割合で取出すことが出来る
ことが分かる。この様にH3B樹脂のゴム量との関係に
おいて相反する性質を示す〔発泡倍率〕と〔割れ量〕の
2つを同時に満足させようとする観点からは第2図に示
す点線の範囲、すなわちH5B樹脂中のゴム成分量が総
ゴム量に対し10〜60重量パーセントの範囲になるよ
う調節することが望ましいことが分る。
That is, it can be seen that improvements in accordance with the target can be extracted by the ratio of the amount of H3B rubber component to the total amount of rubber component in the composition. In this way, from the viewpoint of simultaneously satisfying the two contradictory properties of [expansion ratio] and [cracking amount] in relation to the rubber amount of H3B resin, the range indicated by the dotted line in Figure 2, that is, H5B It has been found that it is desirable to adjust the amount of rubber component in the resin to be in the range of 10 to 60 percent by weight based on the total amount of rubber.

上述した様に、本発明の発泡用樹脂組成物の発泡成形体
によれば、全樹脂量に占める総ゴム成分量が少ない量で
も極めて高い〔耐割れ性〕と優れた〔圧縮歪の回復性〕
とを有するものが得られると言う効果が究明された。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
ないが、以下の様に考えられる。すなわち、 0発泡用
樹脂組底物を構成するHIPS樹脂とHSB樹脂が相互
に相溶性が高く均質に良く混合すること、 ■主体とな
る)flPs樹脂自体が高い剛性と耐割れ性を備えてい
ること。 ■用いるH3B樹脂が、極めて高い耐割れ性
をもつこと。これらの性質をもつHIPS樹脂とH3B
樹脂の均質混合によってもたらされる相乗効果であろう
と考えられている。
As mentioned above, according to the foam molded article of the foamable resin composition of the present invention, even if the total amount of rubber components in the total amount of resin is small, it has extremely high [cracking resistance] and excellent [compressive strain recovery]. ]
The effect of obtaining a product having the following properties was investigated. Although the mechanism by which such an effect occurs is not necessarily clear, it is thought to be as follows. In other words, the HIPS resin and HSB resin that make up the zero-foamed resin bottom are highly compatible with each other and mix well and homogeneously; ■The main component of the flPs resin itself has high rigidity and crack resistance. thing. ■The H3B resin used has extremely high cracking resistance. HIPS resin and H3B with these properties
It is believed that this is a synergistic effect brought about by homogeneous mixing of the resins.

ついで第1表は本発明でいうHIPS樹脂とH3B樹脂
とを採用する意義を示すものである。又結果的には従来
技術と照らして、本発明の効果を端的に示すものである
。すなわち、本発明の樹脂組成物とそれから得られた発
泡成形体によれば、実施例1に見られるように、全ての
評価項目において極めて劣るという評価(表中×印で記
載)されるものは見られず、全樹脂量に対する総ゴム成
分の割合いの広い範囲で優れた性能を示すものである。
Next, Table 1 shows the significance of employing HIPS resin and H3B resin in the present invention. Furthermore, the results clearly demonstrate the effects of the present invention in comparison with the prior art. That is, according to the resin composition of the present invention and the foamed molded product obtained therefrom, as seen in Example 1, those that were evaluated as extremely poor in all evaluation items (indicated by an x in the table) were It shows excellent performance over a wide range of the ratio of the total rubber component to the total resin amount.

尚、実用的には、全樹脂量に対する総ゴム成分の割合い
が10〜25重量パーセントの範囲から選ぶことが望ま
しい事実を示すものである。
This indicates the fact that, practically, it is desirable to select the ratio of the total rubber component to the total resin amount from a range of 10 to 25 weight percent.

本発明で用いられるHIPS樹脂は、特に制限されるも
のでなく一般に用いられているゴム成分量が全HIPS
樹脂量に対し3〜15重量パーセントであるものが好ま
しい、又、用いられるH3B樹脂は、好ましくは、全H
3B樹脂量に占めるビニル芳香族化合物成分の量が20
〜80重量パーセントでかつ共役ジエンに由来する2重
粘合の水素添加による飽和度が好ましくは80パ一セン
ト以上、さらに好ましくは90パ一セント以上のものの
中から選定されるのが良い、ビニル芳香族化合物成分の
量が20重量パーセント未満ではややHIPS樹脂との
混りが悪く均質な混合物が得にくく、又ビニル芳香族化
合物成分の量が80重量パーセントを越ると高価な1(
SB樹脂を加える量が多くなりコスト面で不利となる。
The HIPS resin used in the present invention is not particularly limited, and the amount of rubber components generally used is the total HIPS resin.
The H3B resin used preferably has a total H3B content of 3 to 15 weight percent based on the amount of resin.
The amount of vinyl aromatic compound component in the amount of 3B resin is 20
~80% by weight and the degree of saturation due to hydrogenation of double viscosity originating from a conjugated diene is preferably 80% or more, more preferably 90% or more. If the amount of the aromatic compound component is less than 20% by weight, mixing with the HIPS resin will be poor and it will be difficult to obtain a homogeneous mixture, and if the amount of the vinyl aromatic compound component exceeds 80% by weight, expensive 1(
The amount of SB resin added increases, which is disadvantageous in terms of cost.

さらに、水素添加される共役ジエン化合物成分の飽和度
が80パ一セント未満では得られるH3B樹脂の剛性が
やや劣る結果、発泡成形体とした時に圧縮強度が低下す
るためである。
Furthermore, if the degree of saturation of the conjugated diene compound component to be hydrogenated is less than 80 percent, the rigidity of the resulting H3B resin will be slightly inferior, resulting in a decrease in compressive strength when formed into a foam molded product.

本発明でいう「全樹脂量に対する総ゴム成分量」及び「
総ゴム成分量に占めるH3BfJ脂のゴム成分量」は、
使用するHIPS樹脂とH3B樹脂の種類及びその配合
を変えて調整することが出来る。
In the present invention, "total rubber component amount relative to total resin amount" and "
The rubber component amount of H3BfJ fat in the total rubber component amount is
It can be adjusted by changing the types of HIPS resin and H3B resin used and their formulation.

本発明では、HIPS樹脂とH3B樹脂を各々求める比
率で配合した後連続的に押出機に供給し、押出機内で加
熱溶融しながら均質に混合し、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
ら回転式カッタで長さ方向にカットし粒子状の発泡用樹
脂組成物を得ることが出来る。
In the present invention, after HIPS resin and H3B resin are blended in the desired ratio, they are continuously fed to an extruder, where they are homogeneously mixed while being heated and melted in the extruder. After extruding it, it is immediately cooled in a cooling bath filled with water, sandwiched between upper and lower drive rolls, and cut lengthwise with a rotary cutter to obtain a particulate foaming resin composition. .

又、本発明の発泡用樹脂組成物から発泡成形体を得る方
法は次の様である。すなわち、前記発泡用樹脂粒子に例
えば、ペンタン、ブタン、モノクロロジフルオロエタン
等の揮発性有機発泡剤を含浸させて発泡性樹脂組成物の
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発泡用樹脂組成物の粒子
を入れ、これに揮発性有機発泡剤を加え満して密閉した
後、加温加圧して含浸させる方法又は当該発泡用樹脂組
成物の粒子を押出機内で加熱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、溶融状態にある発泡用樹脂組成物と十分混合し、そ
の後押出機のグ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、発泡性樹脂組成物の粒子を得る方法が用いら
れる。
Further, the method for obtaining a foamed molded article from the foamable resin composition of the present invention is as follows. That is, the particles of the foamable resin composition are obtained by impregnating the foamable resin particles with a volatile organic foaming agent such as pentane, butane, monochlorodifluoroethane, or the like. The method of impregnating the volatile organic blowing agent is, for example, by placing the particles of the foaming resin composition in an autoclave, adding the volatile organic blowing agent to the autoclave, sealing it, and impregnating it by heating and pressurizing it. Alternatively, after the particles of the foaming resin composition are heated and melted in an extruder, a volatile organic foaming agent is separately press-injected through a foaming agent supply line leading to the extruder, and the volatile organic foaming agent is thoroughly mixed with the molten foaming resin composition. After that, it is extruded into a thread form through the pores provided in the goo part of the extruder, and while it is cooled directly in a cooling bath filled with water, it is sandwiched between upper and lower drive rolls and taken out, while being cut lengthwise with a rotary cutter. A method of cutting and obtaining particles of the foamable resin composition is used.

つぎにこれら発泡性樹脂組成物の粒子を公知のポリスチ
レン発泡ビーズ用発泡機でスチームを用いて加熱発泡し
発泡粒子となす。尚得られる発泡粒子の発泡倍率は発泡
機に投入する発泡性樹脂組成物の粒子の重量に対し、該
発泡性樹脂粒子が発泡機内で目標とする体積に膨張した
時に自動的にスチームの供給を止め発泡を停止し目標と
する発泡倍率を得るものである。
Next, the particles of the foamable resin composition are heated and foamed using steam in a known foaming machine for polystyrene foam beads to form foamed particles. The expansion ratio of the resulting foamed particles is determined by automatically supplying steam when the foamable resin particles expand to a target volume in the foaming machine, relative to the weight of the particles of the foamable resin composition charged into the foaming machine. This is to stop foaming and obtain the target foaming ratio.

さらに得られた発泡粒子を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。
Further, the obtained expanded beads are fused and integrated into a single piece using a known automatic molding machine for polystyrene expanded beads to obtain a expanded molded product.

〔実施例〕〔Example〕

次に実施例を挙げて本発明を説明する。 Next, the present invention will be explained with reference to Examples.

なお、以下の実施例及び比較例における測定方法及び評
価方法は下記の通りである。
Note that the measurement methods and evaluation methods in the following Examples and Comparative Examples are as follows.

〈測定方法〉 発泡倍率 およそ5gの発泡粒子を少数以下2位まで秤量し正確な
重量(W>を求める。次に最小目盛単位がlccである
ガラス製メスシリンダにおよそ50〜100ccの水を
入れ、これに先端がメスシリンダの口径よりやや小さい
円形の金網板であってその中心部に長さがおよそ15〜
30cmの針金が固定し直立した発泡ビーズの押圧具を
没しその時の水位(Vo)を読み取る。
<Measurement method> Weigh foamed particles with an expansion ratio of approximately 5g to the second decimal place to determine the accurate weight (W>.Next, pour approximately 50 to 100cc of water into a glass measuring cylinder whose minimum scale unit is lcc. In addition to this, there is a circular wire mesh plate whose tip is slightly smaller than the diameter of the female cylinder, and in the center there is a wire mesh plate with a length of approximately 15 to 15 mm.
A 30 cm wire is fixed to the upright foam bead pressing tool, and the water level (Vo) at that time is read.

次に、押圧具を除き重量を確めている発泡粒子をメスシ
リンダー内に入れ押圧具で完全に水没させた状態で再び
水位(V)を読み取り以下により発泡倍率を求めた。
Next, the foamed particles whose weight had been confirmed with the pressing tool removed were placed in a graduated cylinder and completely submerged in water using the pressing tool, and the water level (V) was again read to determine the foaming ratio.

発泡剤含有量 およそ5gの発泡性樹脂粒子を、重量が小数以下2位ま
で秤量し確められている上部が開放され、寸法形状が、
低面積78.5cn!で高さが10cmの円筒形状のガ
ラス容器に移し、同様に小数以下2位まで秤量して重量
を確める。さらに該樹脂粒子をガラス容器と共に100
℃に制御されている真空脱気装置に入れ真空度−700
mm11g下で60分間脱気した後取り出し室内で5分
間放置冷却後、小数以下2位まで秤量し重量を確め以下
の様に求めた。
The upper part of the foamable resin particles with a foaming agent content of approximately 5g is weighed to two decimal places and the size and shape are as follows.
Low area 78.5cn! Transfer it to a cylindrical glass container with a height of 10 cm, and weigh it in the same way to two decimal places to confirm the weight. Further, the resin particles were added together with the glass container to 100%
Place in a vacuum deaerator controlled at ℃ -700 vacuum degree
After degassing under 11 g of mm for 60 minutes, the sample was taken out and allowed to cool for 5 minutes in a room, and then weighed to two decimal places to determine the weight as shown below.

G :発泡剤含有量(g/100g樹脂)GOニガラス
容器の重量(g) G1:初期のガラス容器とサンプルの合計重量(g) G2:真空脱気後のガラス容器とサンプルの合計重量(
g) G+’Ly。
G: Blowing agent content (g/100g resin) Weight of GO Ni glass container (g) G1: Total weight of initial glass container and sample (g) G2: Total weight of glass container and sample after vacuum degassing (
g) G+'Ly.

割れ量 J I 5−Z−0235、落下衝撃試験法に準じ第3
図に示すごとく厚み寸法■が5 cmである板状発泡成
形体1の上面から60cmの高さから、錘り3と1体と
なっている木製の形状が直方体の落下衝撃体2を板状発
泡成形体1の長さ方向にはほぼ中央部に、巾方向には全
面にわたるように落下し、この時発生する板状発泡成形
体1の最大圧縮歪量と割れ寸法■の関係を求めた。さら
に、これらの関係を明確にするために最大圧縮歪量を横
軸に、又割れ寸法■を縦軸に取りグラフ上に整理した。
Crack amount J I 5-Z-0235, 3rd grade according to drop impact test method
As shown in the figure, from a height of 60 cm from the top surface of the plate-shaped foamed molded body 1 whose thickness dimension ■ is 5 cm, the wooden shaped rectangular parallelepiped drop impact body 2, which is integrated with the weight 3, is dropped into a plate-like shape. The foamed molded product 1 fell approximately at the center in the length direction and over the entire width in the width direction, and the relationship between the maximum compressive strain of the plate-shaped foamed molded product 1 that occurs at this time and the crack size ■ was determined. . Furthermore, in order to clarify these relationships, the maximum compressive strain amount was plotted on the horizontal axis, and the crack size (■) was plotted on the vertical axis, and they were arranged on a graph.

つぎに得られたグラフから板状発泡成形体1の元の厚み
寸法■に対し最大圧縮歪量が60パ一セント時の割れ寸
法を求め、次の様に割れ量を求めた。
Next, from the obtained graph, the crack size when the maximum compressive strain amount was 60 percent with respect to the original thickness size (■) of the plate-shaped foam molded product 1 was determined, and the amount of crack was determined as follows.

S:割れ量(%) H:割れ寸法(cm) T:板状発泡成形体の厚み寸法(cm)S=    X
100 圧遣jソ■側見量 JIS  K−6767繰返し圧縮永久歪試験法に準じ
縦×横×厚さ寸法が各々50mm X 50mm X 
50mmの試験体を25%圧縮試験を行い以下の様に求
めた。
S: Amount of cracks (%) H: Crack size (cm) T: Thickness size of plate-shaped foam molded product (cm) S=X
100 Pressure j So ■ Side viewing amount According to JIS K-6767 cyclic compression set test method, length x width x thickness dimensions are each 50 mm x 50 mm x
A 25% compression test was performed on a 50 mm specimen, and the results were determined as follows.

R:圧縮永久歪の回復量(閣) RI:25%圧縮時の厚み寸法(mm)R2:回復後の
厚み寸法(mm) R=R,−R。
R: Recovery amount of compression set (Kaku) RI: Thickness dimension at 25% compression (mm) R2: Thickness dimension after recovery (mm) R=R, -R.

圧箱五度 JIS  Z−0234圧縮試験法に基き、縦×横×厚
み寸法が100mmX 100mmX 50+nn+。
Based on the pressure box 5 degree JIS Z-0234 compression test method, length x width x thickness dimensions are 100mm x 100mm x 50+nn+.

の試験体を厚み方向に毎分10mmの速度で圧縮し、厚
みに対し25%の圧縮歪を生じた時の圧縮応力値(kg
/cn)を圧縮強度とする。
The compressive stress value (kg
/cn) is the compressive strength.

〈評価方法〉 ’    t A) 発泡剤としてペンタンを100gの樹脂に対し10g量
含浸してなる発泡性樹脂組成物の粒子を発泡ビーズポリ
スチレン用発泡機(積水工機製作所社製、5KK−50
)にてスチーム温度98℃で50秒間加熱発泡した後5
0℃の乾燥器内で20分間乾燥後、発泡倍率の測定方法
によって発泡倍率を確認し、以下の様に求めた。
<Evaluation method>'t A) Particles of a foamable resin composition obtained by impregnating 10 g of pentane as a blowing agent into 100 g of resin using a foaming machine for foaming bead polystyrene (manufactured by Sekisui Koki Seisakusho Co., Ltd., 5KK-50).
) for 50 seconds at a steam temperature of 98°C, then
After drying in a drying oven at 0° C. for 20 minutes, the foaming ratio was confirmed using the foaming ratio measuring method, and was determined as follows.

〔評価尺度〕[Evaluation scale]

前記、高発泡性能の評価の項で用いたのと同一の発泡性
樹脂粒子を発泡ビーズポリスチレン用発泡機(積木工種
製作所社製、5KK−50)にて30倍の発泡粒子とし
た後、該発泡粒子を乾燥機によってほぼ完全に湿度が除
かれている室温の容器内におよそ24時間放置し、はぼ
完全に発泡粒子表面及び内部の湿分を除いた後取り出し
、直ちに発泡剤含有量の測定方法によって発泡剤含有量
を確めた。さらに3時間毎に同様の方法で発泡剤含有量
を確認し放置時間と発泡剤含有量の関係を図示し、発泡
剤含有量が8 (g/100g樹脂)から4(g/10
0g樹脂)まで半減する時の所要時間を確認し、以下の
様に発泡剤保持性能を求めた。
The same foamable resin particles used in the evaluation section of high foaming performance were made into 30 times larger foam beads using a foaming machine for foamed bead polystyrene (5KK-50, manufactured by Chiboku Kotane Seisakusho Co., Ltd.). The foamed particles are left in a container at room temperature from which humidity has been almost completely removed using a dryer for approximately 24 hours, and after almost completely removing moisture on the surface and inside of the foamed particles, the particles are taken out and the foaming agent content is immediately reduced. The blowing agent content was determined by the measuring method. Furthermore, the blowing agent content was confirmed in the same manner every 3 hours, and the relationship between the standing time and the blowing agent content was shown.
The time required to reduce the amount by half to 0g resin) was confirmed, and the foaming agent retention performance was determined as follows.

〔評価尺度〕[Evaluation scale]

前記、発泡剤保持性能の評価の項で用いたと同一の発泡
粒子を発泡ビーズポリスチレン用自動床形機(笠原工業
■製、PIONY−75)を用いて板状発泡成形体(縦
×横×厚さの寸法が300mm X 300mm X 
50mmで嵩密度が25kg/m”)を成形し、前記、
割れ量の測定方法によって以下の様に求めた。
The same foamed particles used in the evaluation of foaming agent retention performance above were used to form a plate-shaped foamed product (length x width x thickness) using an automatic bed forming machine for foamed beaded polystyrene (manufactured by Kasahara Kogyo ■, PIONY-75). Dimensions are 300mm x 300mm x
50 mm and a bulk density of 25 kg/m"), and
The amount of cracking was determined as follows using the measurement method.

〔評価尺度〕[Evaluation scale]

上記、耐割れ性能の評価の項で用いたと同一の発泡成形
体について前記圧縮強度の測定方法によって以下の様に
求めた。
The compressive strength of the same foamed molded product used in the evaluation of crack resistance performance was determined as follows using the method described above.

〔評価尺度〕[Evaluation scale]

圧縮歪の回復性能(効果E) 前記、割れ性能の評価で用いたと同一の発泡成形体を用
い、前記圧縮歪の回復量の測定方法によって以下の様に
求めた。
Compressive Strain Recovery Performance (Effect E) Using the same foamed molded body as used in the evaluation of cracking performance, the compressive strain recovery was determined as follows using the method described above.

〔評価尺度〕[Evaluation scale]

総合評価 実施例1 この実験は、本発明でいう発泡用樹脂組成物に揮発性有
機発泡剤を含浸し発泡性樹脂組成物を得た時、得られた
発泡性樹脂組成物が、高い発泡性能と発泡剤保持性能を
備え、かつこれら発泡性樹脂粒子から得られる発泡成形
体が優れた耐割れ性と圧縮強度特性及び圧縮歪の回復性
を有するという事実を立証しようとするものである。
Comprehensive Evaluation Example 1 In this experiment, when a foamable resin composition was obtained by impregnating a foamable resin composition in the present invention with a volatile organic blowing agent, the resulting foamable resin composition showed high foaming performance. The purpose of this study is to prove that foam molded articles obtained from these expandable resin particles have excellent cracking resistance, compressive strength characteristics, and compressive strain recovery.

HIPS樹脂〔旭化成工業■製、商品名;スタイロン−
HIPS)と水素添加される共役ジエン化合物成分の飽
和度が99パ一セント以上であるH3B樹脂〔旭化威工
業■製、商品名;タフチック〕を実験番号の順に実験番
号と対応する組成化に各々配合し、各々毎にドラム式ブ
レンダーで良く混合した後、当該混合樹脂を各々別に押
出機内で溶融混練しダイ部に設けられた細孔から糸状に
押出し、直ちに冷却水を貯えた冷却バスを介して冷却し
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用樹脂組成物の粒子を
得た。次に、これら粒子を実験番号の順に別々に発泡剤
の加圧供給装置をもち、かつその加圧供給装置からの接
続ラインが押出機シリンダー内、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
樹脂の流出孔をもつグ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
置からペンタンを、樹脂100重量部に対し10重量部
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グ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、はぼ室温であ
る水を貯えた冷却バスを介して上下2本の駆動ロールに
挟み引取りながら回転式カッターにて長さ方向にカット
し、寸法がおよそ径1.0 m、長さ4.0 Inの発
泡性樹脂組成物の粒子を得た。これら発泡性樹脂組成物
の粒子から既述の方法により、発泡性樹脂組成物の粒子
及び発泡成形体を得、評価した。評価結果を第1表に示
す。
HIPS resin [manufactured by Asahi Kasei Corporation, product name: Styron]
HIPS) and H3B resin (manufactured by Asahi Kaei Kogyo ■, trade name: Toughtic) whose saturation degree of the conjugated diene compound component to be hydrogenated is 99 percent or more were made into compositions corresponding to the experiment numbers in the order of experiment numbers. After mixing each resin well with a drum blender, the mixed resins are individually melted and kneaded in an extruder, extruded into threads through the pores in the die, and immediately put into a cooling bath containing cooling water. While being cooled through the medium, the mixture was sandwiched between upper and lower drive rolls, and then cut in the length direction with a rotary cutter to obtain particles of a foamable resin composition. Next, these particles are separately placed in the order of the experiment number with a pressurized blowing agent supply device, and the connection line from the pressurized feed device is connected to the inside of the extruder cylinder and the melt-kneading section. The resin is fed to an extrusion impregnation device equipped with a resin cooling device and a Goo device with a large number of resin outflow holes in the head, and while melting and kneading in the extruder, pentane is added from the blowing agent pressurized feeding device to 100% resin by weight. 10 parts by weight with a pump, and while kneading and mixing with the resin, cooled to an appropriate temperature in a cooling device, extruded into thread form from a number of pores provided in the Gui device, and immediately, The material was passed through a cooling bath containing water at about room temperature and then taken between two drive rolls (upper and lower) and cut lengthwise with a rotary cutter, resulting in a diameter of approximately 1.0 m and a length of 4.0 m. Particles of a foamable resin composition of 0 In were obtained. From these particles of the foamable resin composition, particles of the foamable resin composition and a foamed molded article were obtained by the method described above and evaluated. The evaluation results are shown in Table 1.

比較例1 ポリスチレン樹脂〔旭化戒工業■製、商品名;スタイロ
ンGP−6803とポリエチレン樹脂〔旭化成工業■製
、サンチックLD−2115)を第2表に示す実験番号
と対応する組成化に各々配合する以外は実施例1と全く
同一の方法で発泡性樹脂組成物の粒子を得、実施例1と
全く同様の方法で評価した。評価結果を第2表に示す。
Comparative Example 1 Polystyrene resin [manufactured by Asahi Kakai Kogyo ■, trade name: Stylon GP-6803] and polyethylene resin [manufactured by Asahi Kasei Kogyo ■, Santic LD-2115] were blended into compositions corresponding to the experiment numbers shown in Table 2. Particles of a foamable resin composition were obtained in the same manner as in Example 1, except for the following steps, and evaluated in the same manner as in Example 1. The evaluation results are shown in Table 2.

比較例2 第2表に示す実験番号に対応するブタジェン底弁を含有
するHIPS樹脂〔旭化戒工業■製、商品名;スタイロ
ン)(I PS)を各々用意し、実施例1と全く同一の
方法で発泡性樹脂組成物の粒子と、発泡成形体を得、実
施例1と全く同様の方法で評価した。評価結果を第2表
に示す。
Comparative Example 2 HIPS resins (manufactured by Asahi Kakai Kogyo, trade name: Styron) (IPS) containing butadiene bottom valves corresponding to the experiment numbers shown in Table 2 were prepared, and HIPS resins identical to those in Example 1 were prepared. Particles of a foamable resin composition and a foamed molded article were obtained by the method, and evaluated in exactly the same manner as in Example 1. The evaluation results are shown in Table 2.

比較例3 HIPS樹脂〔旭化或工業■製、商品名;スタイロン−
HIPS、ゴム成分含有量7型量パーセント〕とSB樹
脂〔旭化戒工業■製、商品名;タフブレン、ゴム成分含
有量50重量パーセント〕を第2表に示す実験番号と対
応する組成比に各々配合し、実施例1と全く同一の方法
で発泡性樹脂組成物の粒子と発泡成形体を得、実施例1
と全く同様の方法で評価した。評価結果を第2表に示す
Comparative Example 3 HIPS resin [manufactured by Asahi Kakogyo ■, product name: Styron-
HIPS, rubber component content 7% by weight] and SB resin [manufactured by Asahi Kakai Kogyo ■, trade name: Toughblane, rubber component content 50% by weight] were respectively added to the composition ratios corresponding to the experiment numbers shown in Table 2. Particles of a foamable resin composition and a foamed molded article were obtained in exactly the same manner as in Example 1.
It was evaluated using exactly the same method. The evaluation results are shown in Table 2.

比較例4 EVA樹脂[三井ポリケミカル■社製、商品名;エバフ
レックスP−607]粒子、水、炭酸マグネシウム、シ
ークミルバーオキサイドを以下の様に配合し、配合中間
液を得た。
Comparative Example 4 EVA resin [manufactured by Mitsui Polychemical ■, trade name: Evaflex P-607] particles, water, magnesium carbonate, and seek mill peroxide were blended as follows to obtain a blending intermediate liquid.

配合中間液の配合比 EVA樹脂        1 、000重量部水  
              2.000   〃炭酸
マグネシウム       5 〃ジークミルパーオキ
サイド   10〃FデシS<ンゼンスル7tン 酸ソ
ーダ        1   〃ついで、上記配合中間
液2,016重量部に、あらかじめ、ベンゾイルパーオ
キサイドを1重量パーセントの濃度で加え溶解してなる
スチレンモノマーを各々以下の様に配合して3種類の配
合液を得た。
Mixing ratio of compounding intermediate liquid EVA resin 1,000 parts by weight water
2.000 Magnesium carbonate 5 Sicumyl peroxide 10 F deciS < 7 tons Sodium acid 1 Next, benzoyl peroxide was added in advance to 2,016 parts by weight of the above blended intermediate solution at a concentration of 1% by weight. The styrene monomers obtained by adding and dissolving the styrene monomers were each blended as follows to obtain three types of blended liquids.

その後、前記配合液21を各々5I!のオートクレーブ
に移し密閉後攪拌しつつ昇温し、温度70℃で5時間保
持し樹脂粒子にスチレンを含浸した後温度を95℃及び
145℃に段階的に昇温し各々の温度で4時間及び30
分間保持し、スチレンの重合反応と同時にスチレンとE
VA樹脂との結合反応を、さらにEVA樹脂の架橋反応
をも行ったのち冷却し、スチレン−EVA共重合樹脂粒
子を取り出した。
After that, each of the above-mentioned compounded liquid 21 was added for 5I! After the autoclave was sealed, the temperature was raised while stirring, and the temperature was maintained at 70°C for 5 hours to impregnate the resin particles with styrene. 30
At the same time as the styrene polymerization reaction, styrene and E
After the bonding reaction with the VA resin and the crosslinking reaction of the EVA resin were performed, the mixture was cooled and the styrene-EVA copolymer resin particles were taken out.

これら樹脂粒子内に含有されたスチレンの量は各々順に
83.75.70重量パーセントであった。尚、これら
スチレン量の求め方は、反応終了後オートクレーブ内に
残留する液中の残留スチレン量を求め、反応前に加えた
スチレン量との差異によってEVA樹脂中に含浸する量
を求ることが出来る。さらに、各々のスチレン−EVA
共重合樹脂粒子2.000gを各々51の耐圧容器に入
れ、ペンタン封入液中で80℃で加圧加温し、該樹脂1
00重量部に対しおよそ15重量部のペンタンを含浸さ
せた後冷却して取り出し発泡性樹脂粒子を得た。つぎに
、これら発泡性樹脂粒子を室温に放置して乾燥しつつ発
泡剤を逸散減少させ既述の発泡剤含有量の確認方法によ
って定期的に継続して発泡剤含有量を確認し、発泡剤含
有量が樹脂100重量部に対しIO重量部に達した時、
実施例と同様に評価した。それらの評価結果を第2表に
示す。
The amount of styrene contained within these resin particles was 83.75.70 weight percent, respectively. The method for determining the amount of styrene is to determine the amount of styrene remaining in the liquid that remains in the autoclave after the reaction is completed, and then determine the amount impregnated into the EVA resin based on the difference from the amount of styrene added before the reaction. I can do it. Furthermore, each styrene-EVA
2.000 g of copolymer resin particles were placed in 51 pressure-resistant containers, heated under pressure at 80°C in a pentane-filled liquid, and the resin 1
After impregnating approximately 15 parts by weight of pentane per 00 parts by weight, the resin particles were cooled and taken out to obtain expandable resin particles. Next, these foamable resin particles are left at room temperature to dry while the blowing agent is dissipated and reduced, and the blowing agent content is checked periodically using the blowing agent content confirmation method described above. When the agent content reaches IO parts by weight per 100 parts by weight of resin,
Evaluation was made in the same manner as in the examples. The evaluation results are shown in Table 2.

比較例5 ポリスチレン樹脂〔旭化或工業@製、商品名;スタイロ
ンGP−680:]を実施例1と同一の方法により発泡
性樹脂粒子を得、実施例1と同様の方法で評価した。評
価結果を第2表に示す。
Comparative Example 5 Expandable resin particles were obtained from polystyrene resin [manufactured by Asahi Kakogyo@, trade name: Stylon GP-680] in the same manner as in Example 1, and evaluated in the same manner as in Example 1. The evaluation results are shown in Table 2.

〔発明の効果〕〔Effect of the invention〕

本発明は、上記の構成を持つことにより、樹脂組成物と
してみたときはこれを発泡体にしようとする時は発泡剤
の保持性に優れ、且つ高発泡成形体を得易いという効果
がある。又、得られた発泡成形体としてみたときは耐割
れ性能、圧縮強度特性、圧縮歪の回復性を兼備し、緩衝
包装用途に優れた発泡成形体であると云う利点があり、
例えば、電子部品、音響機器又は通信機器等の軽量でか
つ破損し易い内容物の緩衝包装に用いることができ、産
業界に果す役割の高い優れた発明である。
By having the above structure, the present invention has the effect that, when viewed as a resin composition, it has excellent retention of a foaming agent when it is intended to be made into a foam, and it is easy to obtain a highly foamed molded product. In addition, when viewed as a foam molded product obtained, it has the advantage of having excellent cracking resistance, compressive strength characteristics, and compressive strain recovery, and is excellent for use in cushioning packaging.
For example, it can be used for cushioning packaging of lightweight and easily damaged contents such as electronic parts, audio equipment, communication equipment, etc., and is an excellent invention that plays a large role in industry.

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

第1図及び第2図は発明の内容を示す実験図である。 第3図は割れ試験法を示す図であり、第3(A)図は錘
り付き落下衝撃体を落下させた時の正面図、第3(B)
図は割れ試験実施後の試験片正面図である。第3図中、
■は発泡成形体、2は落下衝撃体、3は錘り、4は発泡
成形体の割れ、■は割れ寸法(ml、■は発泡成形体の
厚み(印)を示す。 HSBのゴム成分V全ゴム成を量 第3 (B)
FIGS. 1 and 2 are experimental diagrams showing the content of the invention. Figure 3 is a diagram showing the cracking test method, Figure 3 (A) is a front view when the weighted drop impact object is dropped, and Figure 3 (B) is a diagram showing the cracking test method.
The figure is a front view of a test piece after conducting a cracking test. In Figure 3,
■ indicates the foam molded product, 2 indicates the drop impact body, 3 indicates the weight, 4 indicates the crack in the foam molded product, ■ indicates the crack size (ml), and ■ indicates the thickness (mark) of the foam molded product. Rubber component V of HSB Amount of total rubber composition 3rd (B)

Claims (1)

【特許請求の範囲】 1、ビニル芳香族化合物と共役ジエン化合物とのブロッ
ク共重体であって共役ジエンに由来する2重結合の大部
分が水素添加され、飽和された共重合樹脂とハイインパ
クトポリスチレン樹脂とを混合してなる発泡用樹脂組成
物。 2、ビニル芳香族化合物と共役ジエン化合物とのブロッ
ク共重合体であって共役ジエンに由来する2重結合の大
部分が水素添加され飽和された共重合樹脂とハイインパ
クトポリスチレン樹脂との混合樹脂組成物で出来た発泡
粒子の多数個を、その表面部で融着一体化させてなる発
泡成形体。
[Claims] 1. A copolymer resin that is a block copolymer of a vinyl aromatic compound and a conjugated diene compound, in which most of the double bonds derived from the conjugated diene are hydrogenated and saturated, and high impact polystyrene. A foaming resin composition made by mixing with resin. 2. A mixed resin composition of a block copolymer of a vinyl aromatic compound and a conjugated diene compound, in which most of the double bonds derived from the conjugated diene are hydrogenated and saturated, and a high impact polystyrene resin. A foamed molded product made by integrating a large number of foamed particles made of a material by fusing them together on the surface.
JP1320567A 1989-12-12 1989-12-12 Foaming resin composition and foamed molded article thereof Expired - Lifetime JP2841303B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1320567A JP2841303B2 (en) 1989-12-12 1989-12-12 Foaming resin composition and foamed molded article thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1320567A JP2841303B2 (en) 1989-12-12 1989-12-12 Foaming resin composition and foamed molded article thereof

Publications (2)

Publication Number Publication Date
JPH03182529A true JPH03182529A (en) 1991-08-08
JP2841303B2 JP2841303B2 (en) 1998-12-24

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ID=18122878

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Country Status (1)

Country Link
JP (1) JP2841303B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994025516A1 (en) * 1993-04-27 1994-11-10 Asahi Kasei Kogyo Kabushiki Kaisha Expanded foamed bead of a rubber-modified styrene polymer
US5580649A (en) * 1993-07-30 1996-12-03 Sekisui Kaseihin Kogyo Kabushiki Kaisha Expandable styrene type resin particles and foamed articles from said particles
EP0706452A4 (en) * 1993-06-22 1997-03-05 Dow Chemical Co POLYSTYRENE FOAM SHEET AND MANUFACTURING METHOD THEREOF
US6232358B1 (en) 1997-09-12 2001-05-15 Mitsubishi Chemical Foam Plastic Corporation Expandable rubber-modified styrene resin compositions
WO2012043792A1 (en) 2010-09-30 2012-04-05 積水化成品工業株式会社 Modified polystyrene resin particles and manufacturing method therefor, expandable particles and manufacturing method therefor, pre-expanded particles, and expanded molded article
WO2012121084A1 (en) 2011-03-04 2012-09-13 積水化成品工業株式会社 Expanded composite polystyrene resin particles and molded foam thereof
CN109476894A (en) * 2016-07-29 2019-03-15 维尔萨利斯股份公司 block expandable polymer composition

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54158467A (en) * 1978-06-05 1979-12-14 Asahi Chem Ind Co Ltd Expandable styrene resin composition
JPS58134863A (en) * 1982-02-01 1983-08-11 日本クラウンコルク株式会社 Plug for vessel
JPS62174237A (en) * 1985-10-19 1987-07-31 Asahi Chem Ind Co Ltd Plyolefin/polystyrene resin mixture foam

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54158467A (en) * 1978-06-05 1979-12-14 Asahi Chem Ind Co Ltd Expandable styrene resin composition
JPS58134863A (en) * 1982-02-01 1983-08-11 日本クラウンコルク株式会社 Plug for vessel
JPS62174237A (en) * 1985-10-19 1987-07-31 Asahi Chem Ind Co Ltd Plyolefin/polystyrene resin mixture foam

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994025516A1 (en) * 1993-04-27 1994-11-10 Asahi Kasei Kogyo Kabushiki Kaisha Expanded foamed bead of a rubber-modified styrene polymer
US5525639A (en) * 1993-04-27 1996-06-11 Asahi Kasei Kogyo Kabushiki Kaisha Expanded foamed bead of a rubber-modified styrene polymer
US5635543A (en) * 1993-04-27 1997-06-03 Asahi Kasei Kogyo Kabushiki Kaisha Expanded foamed bead of a rubber-modified styrene polymer
CN1038843C (en) * 1993-04-27 1998-06-24 旭化成工业株式会社 Expanded foamed beads of rubber-modified styrene polymer, production method and use thereof
CN1067625C (en) * 1993-04-27 2001-06-27 旭化成工业株式会社 Expanded foamed bead of rubber-modified styrene polymer
EP0706452A4 (en) * 1993-06-22 1997-03-05 Dow Chemical Co POLYSTYRENE FOAM SHEET AND MANUFACTURING METHOD THEREOF
US5580649A (en) * 1993-07-30 1996-12-03 Sekisui Kaseihin Kogyo Kabushiki Kaisha Expandable styrene type resin particles and foamed articles from said particles
US6232358B1 (en) 1997-09-12 2001-05-15 Mitsubishi Chemical Foam Plastic Corporation Expandable rubber-modified styrene resin compositions
WO2012043792A1 (en) 2010-09-30 2012-04-05 積水化成品工業株式会社 Modified polystyrene resin particles and manufacturing method therefor, expandable particles and manufacturing method therefor, pre-expanded particles, and expanded molded article
US9127148B2 (en) 2010-09-30 2015-09-08 Sekisui Plastics Co., Ltd. Modified polystyrene resin particles and manufacturing method therefor, expandable particles and manufacturing method therefor, pre-expanded particles, and expanded molded article
WO2012121084A1 (en) 2011-03-04 2012-09-13 積水化成品工業株式会社 Expanded composite polystyrene resin particles and molded foam thereof
US9127135B2 (en) 2011-03-04 2015-09-08 Sekisui Plastics Co., Ltd. Expanded composite polystyrene-based resin particles and expanded molded article thereof
CN109476894A (en) * 2016-07-29 2019-03-15 维尔萨利斯股份公司 block expandable polymer composition
JP2019523310A (en) * 2016-07-29 2019-08-22 ベルサリス、ソシエタ、ペル、アチオニVersalis S.P.A. Block foamable polymer composition
CN109476894B (en) * 2016-07-29 2021-05-25 维尔萨利斯股份公司 block expandable polymer composition
US11078342B2 (en) * 2016-07-29 2021-08-03 Versalis S.P.A. Block expandable polymeric compositions

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