JP2012207165A - Method for manufacturing expansion molding, and expansion molding - Google Patents

Method for manufacturing expansion molding, and expansion molding Download PDF

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JP2012207165A
JP2012207165A JP2011075097A JP2011075097A JP2012207165A JP 2012207165 A JP2012207165 A JP 2012207165A JP 2011075097 A JP2011075097 A JP 2011075097A JP 2011075097 A JP2011075097 A JP 2011075097A JP 2012207165 A JP2012207165 A JP 2012207165A
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particles
bulk
foamed molded
resin
molded article
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Takashi Motomura
隆司 本村
Kazuo Tajima
一雄 田島
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Sekisui Kasei Co Ltd
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Sekisui Plastics Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a simple method for manufacturing an expansion molding, having a high expansion ratio and excellent in strength.SOLUTION: The method for manufacturing an expansion molding include expansion-molding a mixture of at least two types of preexpanded particles having different bulk expansion ratios, wherein the mixture contains at least a first preexpanded particle having a first bulk expansion ratio (X) of 30 to 80 and a second preexpanded particle having a second bulk expansion ratio of X+5 to X+30 times.

Description

本発明は、発泡成形体の製造方法及び発泡成形体に関する。更に詳しくは、本発明は、魚介類や農産物等を収容し、保管あるいは輸送する際に用いられる、高倍数で、強度に優れた発泡成形体の簡便な製造方法及び前記の製造方法より得られる発泡成形体に関する。   The present invention relates to a method for producing a foam molded article and a foam molded article. More specifically, the present invention is obtained from a simple method for producing a foamed molded article having high strength and excellent strength, which is used when storing, storing or transporting seafood, agricultural products and the like, and the aforementioned production method. The present invention relates to a foam molded article.

発泡スチロール材等の合成樹脂からなる製品は、断熱性を備えている上に、更に、軽量で成型がしやすく、衝撃吸収性にも優れているという特性を有する。このため、従来から、これらは、野菜、果物、肉類、魚介類等を保管あるいは輸送する際に使用する容器として汎用されている。   A product made of a synthetic resin such as a polystyrene foam material has heat insulating properties, light weight, easy molding, and excellent impact absorption. For this reason, conventionally, these have been widely used as containers used for storing or transporting vegetables, fruits, meats, seafood and the like.

また、これらは原料となる発泡性樹脂粒子を何倍の大きさに膨らませるか、いわゆる製品の倍数の大きさを変化させることによって、その性質は大きく変わる。このため、これらの製品はその倍数に従って、その用途を変えて使用されている。   In addition, the properties of these expandable resin particles vary greatly depending on how many times the expandable resin particles are expanded, or by changing the size of a so-called product. For this reason, these products are used in different applications according to the multiple.

更に、発泡性樹脂粒子を大きく膨らませれば膨らませるほど、合成樹脂材の量は少なくて済む。このため、製品を安価に製造することもできる。しかしながら、製品の倍数を大きくすればするほど、その強度は弱くなる。そこで、特許文献1には、容器の形状を変えることで引張強度を向上させた、合成樹脂からなる容器及びその製造方法が記載されている。   Furthermore, the more the expandable resin particles are expanded, the smaller the amount of the synthetic resin material. For this reason, a product can also be manufactured cheaply. However, the greater the product multiple, the weaker the strength. Therefore, Patent Document 1 describes a container made of a synthetic resin, which has improved tensile strength by changing the shape of the container, and a method for manufacturing the same.

特開2010−274980号公報JP 2010-274980 A

魚介類や農産物等の保管、輸送用として使用する発泡成形体は、一般的に50〜60倍の倍数が好適とされ、この数値内で製品化されたものが市場に出回っているが、より一層の軽量化及び使用に耐えられる強度を備えた容器の開発が求められている。   The foamed molded product used for storage and transportation of seafood, agricultural products, etc. is generally preferred to be a multiple of 50-60 times, and products that have been commercialized within this value are on the market. There is a demand for the development of a container having a strength that can withstand further weight reduction and use.

しかしながら、前記の観点からは、従来の発泡成形体や特許文献1に記載の発泡成形体は満足のいくものではなかった。特に、発泡成形体の倍数を上げつつ、特許文献1に記載のように形状を変更した場合、一定の強度の向上は認められるものの、軽量化と強度との両立という観点からは必ずしも満足のいくものではなかった。具体的には、強度の向上を目的として発泡成形体の形状を変更した場合、発泡成形体の形状によっては所定の方向での強度向上は図れることがあるものの、全ての方向において強度の向上を図ることができないことがあった。このような場合、発泡成形体、特に保管、輸送用の容器は、使用時の衝撃や振動に抗し切れず、破損等を起こすことがある。   However, from the above viewpoint, the conventional foam molded article and the foam molded article described in Patent Document 1 have not been satisfactory. In particular, when the shape is changed as described in Patent Document 1 while increasing the multiple of the foamed molded article, although a certain improvement in strength is recognized, it is not always satisfactory from the viewpoint of achieving both weight reduction and strength. It was not a thing. Specifically, when the shape of the foamed molded product is changed for the purpose of improving the strength, the strength may be improved in a predetermined direction depending on the shape of the foamed molded product, but the strength is improved in all directions. I was unable to plan. In such a case, the foamed molded product, particularly the container for storage and transportation, cannot withstand the shock and vibration during use and may be damaged.

このため、発泡成形体全体において高い強度を示すような、高倍数で、強度に優れた発泡成形体の提供が課題とされている。また、そのような発泡成形体の簡便な製造方法の提供も課題とされている。   For this reason, it is an object to provide a foamed molded article having high strength and high strength that exhibits high strength throughout the foamed molded article. In addition, provision of a simple method for producing such a foam-molded product is also an issue.

かくして本発明によれば、嵩倍数の異なる少なくとも2種の予備発泡粒子の混合物を発泡成形することにより得られ、前記混合物が30〜80倍の第1の嵩倍数(X)を有する第1予備発泡粒子とX+5〜X+30倍の第2の嵩倍数を有する第2予備発泡粒子とを少なくとも含むことを特徴とする発泡成形体の製造方法が提供される。   Thus, according to the present invention, the first preliminary obtained by foam-molding a mixture of at least two kinds of pre-expanded particles having different bulk ratios, wherein the mixture has a first bulk ratio (X) of 30 to 80 times. There is provided a method for producing a foamed molded article, comprising at least foamed particles and second pre-foamed particles having a second bulk multiple of X + 5 to X + 30.

また、本発明によれば、前記製造方法により得ることができる発泡成形体も提供される。   Moreover, according to this invention, the foaming molding which can be obtained with the said manufacturing method is also provided.

本発明においては、使用原料として、低嵩倍数の予備発泡粒子と高嵩倍数の予備発泡粒子とを用いるため、それらの混合物から得られる発泡成形体は両者に由来する特性を最大限に引き出すことができる。
従って、本発明によれば、高倍数で、強度に優れた発泡成形体の簡便な製造方法を提供できる。
In the present invention, low-bulk multiple pre-expanded particles and high-bulk multiple pre-expanded particles are used as raw materials, so that the foam molded product obtained from the mixture can maximize the characteristics derived from both. Can do.
Therefore, according to the present invention, it is possible to provide a simple method for producing a foamed molded article having a high multiple and excellent strength.

また、本発明によれば、発泡成形体が樹脂成分としてポリスチレン系樹脂を含む場合、ポリスチレン系樹脂は発泡性により優れるため、更により高倍数で、強度に優れた発泡成形体の簡便な製造方法を提供できる。   Further, according to the present invention, when the foamed molded article contains a polystyrene resin as a resin component, the polystyrene resin is more excellent in foaming property, and therefore, a simpler method for producing a foamed molded article having higher strength and strength. Can provide.

本発明によれば、高倍数で、強度に優れた発泡成形体を提供することもできる。   According to the present invention, it is possible to provide a foamed molded article having a high multiple and excellent strength.

また、本発明によれば、箱形状であるような高倍数で、強度に優れた発泡成形体を提供することもできる。   In addition, according to the present invention, it is possible to provide a foamed molded article having a high multiple such as a box shape and excellent strength.

本発明の特徴は、嵩倍数の異なる少なくとも2種の予備発泡粒子の混合物を発泡成形することにより得られ、前記混合物が30〜80倍の第1の嵩倍数(X)を有する第1予備発泡粒子とX+5〜X+30倍の第2の嵩倍数を有する第2予備発泡粒子とを少なくとも含む発泡成形体の製造方法である。   The feature of the present invention is obtained by foam-molding a mixture of at least two kinds of pre-expanded particles having different bulk ratios, and the mixture has a first bulk ratio (X) of 30 to 80 times. It is a manufacturing method of the foaming molding which contains particle | grains and the 2nd pre-expanded particle | grains which have a 2nd bulk factor of X + 5-X + 30 times.

具体的には、発泡成形体の原料として、嵩倍数の異なる少なくとも2種以上の予備発泡粒子の混合物を使用する。より具体的には、発泡成形体の原料として、30〜80倍の第1の嵩倍数(X)を有する第1予備発泡粒子とX+5〜X+30倍の第2の嵩倍数を有する第2予備発泡粒子とを少なくとも含む予備発泡粒子の混合物を使用する。このため、耐衝撃性や耐熱性に優れた比較的嵩倍数の低い予備発泡粒子と、高倍数の発泡成形体を得ることができる比較的嵩倍数の高い予備発泡粒子とを少なくとも含む予備発泡粒子の混合物を使用することによって、これらの特性を維持しつつ、発泡成形体を製造できる。   Specifically, a mixture of at least two types of pre-expanded particles having different bulk ratios is used as a raw material for the foam molded article. More specifically, as the raw material of the foam molded article, the first pre-expanded particles having a first bulk factor (X) of 30 to 80 times and the second pre-foaming having a second bulk factor of X + 5 to X + 30 times. A mixture of pre-expanded particles comprising at least particles is used. Therefore, pre-expanded particles comprising at least pre-expanded particles having a relatively low bulk ratio and excellent impact resistance and heat resistance, and pre-expanded particles having a relatively high bulk ratio capable of obtaining a high-magnification expanded molded article. By using the mixture, it is possible to produce a foam molded article while maintaining these characteristics.

従って、本発明によれば、高倍数で、強度に優れた発泡成形体の簡便な製造方法を提供できる。
以下、本発明の樹脂粒子の製造方法及び本発明の製造方法によって得られる発泡成形体について詳説する。
Therefore, according to the present invention, it is possible to provide a simple method for producing a foamed molded article having a high multiple and excellent strength.
Hereinafter, the method for producing resin particles of the present invention and the foam molded article obtained by the production method of the present invention will be described in detail.

本発明の発泡成形体は、
(1)発泡剤を樹脂粒子に含浸させる含浸工程(発泡性樹脂粒子の製造工程)と、
(2)発泡性樹脂粒子を予備発泡させる予備発泡工程(予備発泡粒子の製造工程)と、
(3)予備発泡粒子を発泡成形する発泡成形工程(発泡成形体の製造工程)とを含む製造方法によって得ることができる。
The foamed molded article of the present invention is
(1) an impregnation step of impregnating the resin particles with the foaming agent (manufacturing step of the expandable resin particles);
(2) a pre-foaming step (pre-foaming particle production step) for pre-foaming the expandable resin particles;
(3) It can be obtained by a production method including a foam molding step (foam molded body production step) for foam-molding pre-expanded particles.

<発泡性樹脂粒子>
本発明において、発泡性樹脂粒子とは、樹脂粒子に所定の割合で発泡剤を含浸させた加熱発泡性能を有する樹脂粒子を意味する。
<Foaming resin particles>
In the present invention, the expandable resin particle means a resin particle having a heat foaming performance in which a resin agent is impregnated with a foaming agent at a predetermined ratio.

(1)樹脂粒子
樹脂粒子を構成する樹脂成分は加熱によって発泡可能であれば特に限定されず、公知の樹脂成分を使用できる。具体的には、ポリスチレン系樹脂、ポリオレフィン系樹脂、ポリ(メタ)アクリル系樹脂、ポリフェニレンエーテル系樹脂、ポリカーボネート系樹脂、ポリエステル系樹脂(例えば、ポリ乳酸系樹脂、PET等)等を挙げることができる。これら樹脂成分は、単独で使用しても、混合して使用してもよい。なお、(メタ)アクリルはアクリル又はメタクリルを意味する。
(1) Resin particle The resin component which comprises a resin particle will not be specifically limited if it can be foamed by heating, A well-known resin component can be used. Specific examples include polystyrene resins, polyolefin resins, poly (meth) acrylic resins, polyphenylene ether resins, polycarbonate resins, polyester resins (for example, polylactic acid resins, PET, and the like). . These resin components may be used alone or in combination. In addition, (meth) acryl means acryl or methacryl.

なお、複数の樹脂成分を使用する場合、使用原料についての、単量体間の質量比率、単量体と樹脂との間の質量比率及び樹脂間の質量比率と、それらから得られる樹脂粒子、予備発泡粒子及び発泡成形体に含まれる樹脂成分の質量比率とは略同一である。   In addition, when using a plurality of resin components, for the raw materials used, the mass ratio between the monomers, the mass ratio between the monomer and the resin and the mass ratio between the resins, and resin particles obtained from them, The mass ratio of the resin component contained in the pre-expanded particles and the expanded molded body is substantially the same.

樹脂成分はポリスチレン系樹脂が好ましい。ポリスチレン系樹脂は高倍の発泡成形体を得ることができるからである。   The resin component is preferably a polystyrene resin. This is because the polystyrene-based resin can obtain a high-magnification expanded molded article.

本発明において、ポリスチレン系樹脂とは、スチレン単独重合体、又はスチレン単量体を主成分とし、スチレン単量体と共重合可能な他の単量体との共重合体を意味する。また、スチレン系単量体とは、スチレン単量体、又はスチレン単量体を主成分とし、スチレン単量体と共重合可能な他の単量体との混合物を意味する。ここでスチレン単量体を主成分とするとは、スチレン単量体が全単量体100質量部に対して80質量部以上を占めることを意味する。
共重合体はランダム共重合体であってよく、ブロック共重合体であってもよい。
In the present invention, the polystyrene resin means a styrene homopolymer or a copolymer of a styrene monomer as a main component and another monomer copolymerizable with the styrene monomer. The styrene monomer means a styrene monomer or a mixture of a styrene monomer as a main component and another monomer copolymerizable with the styrene monomer. Here, the styrene monomer as a main component means that the styrene monomer occupies 80 parts by mass or more with respect to 100 parts by mass of all monomers.
The copolymer may be a random copolymer or a block copolymer.

また、スチレン単量体と共重合可能な他の単量体として、α−メチルスチレン、p−メチルスチレン、アクリロニトリル、メタクリロニトリル、アクリル酸、メタクリル酸、アクリル酸アルキルエステル、メタクリル酸アルキルエステル、ジビニルベンゼン及びポリエチレングリコールジメタクリレートのようなビニル系単量体を挙げることができる。本発明において、アルキルとは炭素数1〜30のアルキルを意味する。
本発明においては、より高倍の発泡成形体を得ることができるため、樹脂成分としてスチレン単独重合体が好ましい。
Further, as other monomers copolymerizable with the styrene monomer, α-methylstyrene, p-methylstyrene, acrylonitrile, methacrylonitrile, acrylic acid, methacrylic acid, alkyl acrylate ester, alkyl methacrylate ester, Mention may be made of vinyl monomers such as divinylbenzene and polyethylene glycol dimethacrylate. In the present invention, alkyl means alkyl having 1 to 30 carbon atoms.
In the present invention, a styrene homopolymer is preferred as the resin component because a higher-magnification foamed molded product can be obtained.

また、ポリスチレン系樹脂は樹脂成分の発泡性確保の観点から、好ましくは20×104〜40×104、より好ましくは25×104〜35×104の平均分子量を有する。なお、本発明において、平均分子量とは、GPC(ゲルパーミエイションクロマトグラフィー)で測定される重量平均分子量を意味する。 The polystyrene resin preferably has an average molecular weight of 20 × 10 4 to 40 × 10 4 , more preferably 25 × 10 4 to 35 × 10 4 from the viewpoint of securing foamability of the resin component. In the present invention, the average molecular weight means a weight average molecular weight measured by GPC (gel permeation chromatography).

樹脂粒子の製造には、公知の重合法、即ち、懸濁重合法、乳化重合法、溶液重合法、シード重合法等を適宜使用できる。また、樹脂成分を樹脂粒子とする際、公知の製造方法及び製造設備をいずれも使用できる。例えば、まず、押出機を使用して樹脂成分を溶融混錬し、押出し、次いで水中カット、ストランドカット等により造粒することによって、樹脂粒子を製造できる。   For the production of the resin particles, a known polymerization method, that is, a suspension polymerization method, an emulsion polymerization method, a solution polymerization method, a seed polymerization method, or the like can be appropriately used. Moreover, when making a resin component into resin particle, both a well-known manufacturing method and manufacturing equipment can be used. For example, resin particles can be produced by first melt-kneading a resin component using an extruder, extruding, and then granulating by underwater cutting, strand cutting or the like.

(2)発泡剤
発泡剤としては、公知の種々の発泡剤が使用できる。例えば、プロパン、n−ブタン(ノルマルブタン)、イソブタン、n−ペンタン(ノルマルペンタン)及びイソペンタンのような炭化水素を挙げることができる。これらの内、より大きな発泡性能を発泡性樹脂粒子に導入できる、n−ブタン、イソブタン、n−ペンタン、イソペンタンのいずれかが好ましい。発泡剤は単独で用いてもよく2種以上を用いてもよい。
(2) Foaming agent Various known foaming agents can be used as the foaming agent. For example, hydrocarbons such as propane, n-butane (normal butane), isobutane, n-pentane (normal pentane) and isopentane can be mentioned. Among these, any of n-butane, isobutane, n-pentane, and isopentane that can introduce greater foaming performance into the foamable resin particles is preferable. A foaming agent may be used independently and may use 2 or more types.

発泡剤の含有率としては、発泡性樹脂粒子100質量部に対して、3〜9質量部であることが好ましい。発泡剤の含有率が3質量部未満であると、発泡性樹脂粒子の発泡性が低下することがある。発泡性が低下すると、嵩倍数の高い低嵩密度の予備発泡粒子が得られ難くなることがある。一方、9質量部を超えると、予備発泡粒子中の気泡サイズが過大となり易く、成形性の低下や、得られる発泡成形体の圧縮、曲げ等の強度特性の低下が発生することがある。より好ましい発泡剤の含有率は、4〜8質量部の範囲である。   As a content rate of a foaming agent, it is preferable that it is 3-9 mass parts with respect to 100 mass parts of expandable resin particles. When the content of the foaming agent is less than 3 parts by mass, the foamability of the foamable resin particles may be lowered. When foamability is lowered, it may be difficult to obtain pre-expanded particles having a high bulk ratio and a low bulk density. On the other hand, when the amount exceeds 9 parts by mass, the bubble size in the pre-expanded particles tends to be excessive, and the moldability may be deteriorated and the strength characteristics such as compression and bending of the obtained foamed molded article may be deteriorated. A more preferable foaming agent content is in the range of 4 to 8 parts by mass.

また、更に均一に発泡性樹脂粒子を予備発泡させ得る発泡助剤を用いてもよい。発泡助剤として、例えば、シクロヘキサン及びd−リモネンのような溶剤、ジイソブチルアジペート、グリセリン、ジアセチル化モノラウレート及びやし油のような可塑剤(高沸点溶剤)を挙げることができる。   Moreover, you may use the foaming auxiliary agent which can pre-expand foamable resin particles more uniformly. Examples of foaming aids include solvents such as cyclohexane and d-limonene, and plasticizers (high boiling solvents) such as diisobutyl adipate, glycerin, diacetylated monolaurate and coconut oil.

(3)その他の原材料
本発明においては、所望の発泡成形体を得ることができる限り、樹脂粒子は他の添加剤等を含んでいてもよい。添加剤として、具体的には、表面処理剤、難燃剤、難燃助剤、被覆剤、連鎖移動剤、光安定剤、紫外線吸収剤、顔料、染料、消泡剤、増粘剤、熱安定剤、レベリング剤、滑剤、帯電防止剤、表面処理剤等が挙げられる。なお、樹脂粒子がこれらの添加剤を含む場合、樹脂粒子から得られる予備発泡粒子、発泡成形体もこれらの添加剤を含む。
(3) Other raw materials In the present invention, the resin particles may contain other additives as long as a desired foamed molded article can be obtained. Specific additives include surface treatment agents, flame retardants, flame retardant aids, coating agents, chain transfer agents, light stabilizers, UV absorbers, pigments, dyes, antifoaming agents, thickeners, and heat stabilizers. Agents, leveling agents, lubricants, antistatic agents, surface treatment agents and the like. In addition, when the resin particle contains these additives, the pre-expanded particles and the foamed molded product obtained from the resin particles also contain these additives.

(4)発泡性樹脂粒子の製造方法
発泡性樹脂粒子は発泡剤を樹脂粒子に含浸させることによって得ることができる。
発泡性樹脂粒子の製造方法は特に限定されず、公知の方法をいずれも用いることができる。
例えば、V型等の回転混合機であって、密閉耐圧の容器に樹脂粒子を入れて流動させ、次いで発泡剤を導入することで樹脂粒子に発泡剤を含浸させる方法や、
攪拌機付密閉耐圧容器内で樹脂粒子を水性媒体に懸濁させ、次いで発泡剤を導入し、樹脂粒子に発泡剤を含浸させる方法を挙げることができる。
(4) Method for Producing Expandable Resin Particles Expandable resin particles can be obtained by impregnating resin particles with a foaming agent.
The production method of the expandable resin particles is not particularly limited, and any known method can be used.
For example, a rotary mixer such as a V-type, in which resin particles are put in a sealed pressure-resistant container and allowed to flow, and then a foaming agent is introduced to impregnate the resin particles with the foaming agent,
A method of suspending resin particles in an aqueous medium in a sealed pressure vessel equipped with a stirrer, then introducing a foaming agent, and impregnating the resin particles with the foaming agent can be mentioned.

また、発泡剤の含浸は80〜120℃、1.0〜7.0時間行うことが好ましい。更に、前記含浸は所望の発泡成形体等を得ることができる限り、加圧条件下で行ってもよい。   The impregnation with the foaming agent is preferably performed at 80 to 120 ° C. for 1.0 to 7.0 hours. Further, the impregnation may be performed under pressure as long as a desired foamed molded article can be obtained.

<予備発泡粒子>
本発明において、予備発泡粒子とは、発泡性樹脂粒子を所定の嵩倍数まで加熱発泡させた樹脂粒子を意味する。
<Pre-expanded particles>
In the present invention, the pre-expanded particles mean resin particles obtained by heating and foaming expandable resin particles to a predetermined bulk factor.

予備発泡粒子は、所望の嵩倍数を有する予備発泡粒子を得ることができる限り、公知の予備発泡方法を用いて製造できる。予備発泡方法の一例を挙げれば、水蒸気等の加熱媒体を用いて発泡性樹脂粒子を加熱し、所定の嵩倍数に予備発泡させることで、予備発泡粒子を得ることができる。   The pre-expanded particles can be produced using a known pre-expand method as long as the pre-expanded particles having a desired bulk factor can be obtained. As an example of the pre-foaming method, the pre-foamed particles can be obtained by heating the foamable resin particles using a heating medium such as water vapor and pre-foaming to a predetermined bulk factor.

本発明においては、より容易に予備発泡を行うことができるため、95〜125℃の水蒸気を用いて発泡性樹脂粒子を予備発泡させることが好ましい。また、予備発泡粒子から水分を除去するために、好ましくは室温で、12時間以上放置してもよい。   In the present invention, since pre-foaming can be performed more easily, it is preferable to pre-foam the expandable resin particles using steam at 95 to 125 ° C. Further, in order to remove moisture from the pre-expanded particles, it may be left at room temperature for 12 hours or more.

本発明の発泡成形体の製造方法では、嵩倍数の異なる少なくとも2種以上の予備発泡粒子の混合物を使用する。本発明においては、このような混合物を使用することによって、高倍数で、強度に優れた発泡成形体を簡便に製造できる。   In the method for producing a foamed molded article of the present invention, a mixture of at least two kinds of pre-expanded particles having different bulk ratios is used. In the present invention, by using such a mixture, a foamed molded article having a high multiple and excellent strength can be easily produced.

具体的には、前記混合物は、30〜80倍、好ましくは40〜70倍、より好ましくは50〜60倍の第1の嵩倍数(X)を有する第1予備発泡粒子を含む。   Specifically, the mixture includes first pre-expanded particles having a first bulk factor (X) of 30 to 80 times, preferably 40 to 70 times, more preferably 50 to 60 times.

また、前記混合物は、X+5〜X+30倍、好ましくはX+8〜X+20倍、より好ましくはX+8〜X+15倍の第2の嵩倍数を有する第2予備発泡粒子も含む。   The mixture also includes second pre-expanded particles having a second bulk factor of X + 5 to X + 30 times, preferably X + 8 to X + 20 times, more preferably X + 8 to X + 15 times.

更に、前記混合物は、より高倍数で、強度に優れた発泡成形体を容易に得ることができるため、第1予備発泡粒子100質量部に対して、好ましくは100〜300質量部、より好ましくは150〜250質量部の割合で第2予備発泡粒子を含む。   Furthermore, since the mixture can easily obtain a foam molded article having a higher magnification and excellent strength, it is preferably 100 to 300 parts by mass, more preferably 100 parts by mass with respect to 100 parts by mass of the first pre-expanded particles. The second pre-expanded particles are included at a ratio of 150 to 250 parts by mass.

他方、前記混合物は、その全体において、好ましくは40〜70倍、より好ましくは45〜65倍の嵩倍数を有する。混合物全体の嵩倍数が40倍より低い場合、軽量化を図ることができないことがある。また、混合物全体の嵩倍数が70倍より高い場合、高い強度を得ることができないことがある。   On the other hand, the mixture as a whole preferably has a bulk factor of 40 to 70 times, more preferably 45 to 65 times. If the bulk ratio of the entire mixture is lower than 40 times, weight reduction may not be achieved. Moreover, when the bulk magnification of the whole mixture is higher than 70 times, high strength may not be obtained.

また、予備発泡粒子の平均粒子径は5.0mm以下が好ましく、4.5mm以下がより好ましい。平均粒子径が5.0mmより大きいと、発泡成形機への予備発泡粒子の充填性が低下することがあり、得られる発泡成形体の強度が低下することがある。なお、本発明においては、予備発泡粒子は、それらの流動性確保の観点から、球状〜略球状(卵状)であることが好ましい。   The average particle diameter of the pre-expanded particles is preferably 5.0 mm or less, and more preferably 4.5 mm or less. When the average particle diameter is larger than 5.0 mm, the filling property of the pre-foamed particles in the foam molding machine may be lowered, and the strength of the obtained foam molded product may be lowered. In the present invention, the pre-expanded particles are preferably spherical to substantially spherical (egg-like) from the viewpoint of ensuring fluidity thereof.

予備発泡粒子の混合は、所望の物性に影響を与えない限り、公知の混合方法、混合機を使用できる。本発明においては、高い嵩倍数の予備発泡粒子を均一に混合できるため、送風機を用いて気流中で混合することが好ましい。   The mixing of the pre-expanded particles can use a known mixing method and mixer as long as the desired physical properties are not affected. In the present invention, since pre-expanded particles having a high bulk ratio can be mixed uniformly, it is preferable to mix them in an air stream using a blower.

<発泡成形体>
本発明の発泡成形体は、上記混合物中の予備発泡粒子を熱融着させ、成形することにより得ることができる。
本発明の発泡成形体は公知の発泡成形方法を用いて製造できる。発泡成形方法の一例を挙げると、公知の発泡成形機の金型内に予備発泡粒子を充填し、再度加熱し、次いで予備発泡粒子同士を熱融着させることにより発泡成形体を得ることができる。加熱用の熱媒体として水蒸気を好適に使用することができる。
<Foamed molded product>
The foamed molded product of the present invention can be obtained by heat-sealing and molding the pre-expanded particles in the above mixture.
The foamed molded product of the present invention can be produced using a known foam molding method. As an example of the foam molding method, it is possible to obtain a foam molded article by filling pre-foamed particles in a mold of a known foam molding machine, heating again, and then thermally fusing the pre-foamed particles together. . Water vapor can be suitably used as the heating medium for heating.

本発明の製造方法によって得られる発泡成形体は、好ましくは50〜70倍、より好ましくは55〜65倍の倍数を有することができる。このことは本発明の発泡成形体は高倍数を有していることを示している。   The foamed molded article obtained by the production method of the present invention can preferably have a multiple of 50 to 70 times, more preferably 55 to 65 times. This has shown that the foaming molding of this invention has a high multiple.

本発明の発泡成形体は箱形状であることが好ましい。この場合、好ましくは140〜300N、より好ましくは140〜200Nの引張強度を有することができる。   The foamed molded product of the present invention is preferably box-shaped. In this case, it can have a tensile strength of preferably 140 to 300 N, more preferably 140 to 200 N.

また、本発明の発泡成形体は好ましくは0〜20%、より好ましくは0〜10%の割れ率を有することができる。このことは本発明の発泡成形体は、箱形状に成形を行った場合であっても、高い強度を有していることを示している。即ち、本発明の発泡成形体はその全体において高い強度を有していることを示している。さらに、発泡成形体の肉厚は15〜30mmの範囲で実施することが好ましく、17〜25mmの範囲がより好ましい。肉厚が15mm未満だと発泡成形機への予備発泡粒子の充填性が低下することがあり、得られる発泡成形体の強度が低下することがある。一方、肉厚が30mmを越えて実施しても容器の重量が重くなることがある。箱形状の寸法として一例をあげると、農産物用の場合は例えば320mm×540mm×高さ250mm、肉厚19mm等の寸法の容器が、水産物用の場合は例えば350×550×高さ150mm、肉厚25mm等の寸法の容器が用いられている。   The foamed molded article of the present invention can preferably have a cracking rate of 0 to 20%, more preferably 0 to 10%. This indicates that the foamed molded article of the present invention has high strength even when molded into a box shape. That is, it shows that the foamed molded product of the present invention has high strength as a whole. Furthermore, it is preferable to implement the thickness of a foaming molding in the range of 15-30 mm, and the range of 17-25 mm is more preferable. When the wall thickness is less than 15 mm, the filling property of the pre-expanded particles in the foam molding machine may be lowered, and the strength of the obtained foam molded body may be lowered. On the other hand, even if the thickness exceeds 30 mm, the weight of the container may increase. As an example of the dimensions of the box shape, a container having dimensions of 320 mm × 540 mm × height 250 mm, a thickness of 19 mm, etc. for agricultural products, for example, 350 × 550 × 150 mm height, thickness for fishery products A container having a size of 25 mm or the like is used.

このため、本発明の製造方法によれば、上面に開口部が設けられた合成樹脂を含む発泡成形体製の容器、特に魚介類や農産物等を収容し、保管あるいは輸送する際等に用いられる上面に開口部が設けられた容器であっても、所望の物性を損なうことなく発泡成形体を製造できる。また、容器の形状を変えず、軽量化(例えば1〜20質量%)を図ったものでありながら、使用に耐え得る引張強度を備えた発泡成形体を製造することもできる。   For this reason, according to the manufacturing method of the present invention, a container made of a foam-molded article containing a synthetic resin having an opening on the upper surface, particularly when storing or transporting seafood, agricultural products, etc. is used. Even in a container having an opening on the upper surface, a foamed molded product can be produced without impairing desired physical properties. Moreover, it is also possible to produce a foamed molded article having a tensile strength that can withstand use while reducing the weight (for example, 1 to 20% by mass) without changing the shape of the container.

従って、本発明によれば、高倍数で、強度に優れた発泡成形体の簡便な製造方法を提供できる。また、本発明の発泡成形体は、包装用緩衝材、建築用部材、自動車部材等として幅広く使用することができ、特に発泡体製容器として使用できる。   Therefore, according to the present invention, it is possible to provide a simple method for producing a foamed molded article having a high multiple and excellent strength. The foamed molded product of the present invention can be widely used as a cushioning material for packaging, a building member, an automobile member, and the like, and can be used particularly as a foam-made container.

以下、実施例を挙げて更に説明するが、本発明はこれら実施例により限定されるものではない。実施例に記載した各種測定法及び製造条件を以下で説明する。   Hereinafter, although an example is given and explained further, the present invention is not limited by these examples. Various measurement methods and production conditions described in the examples will be described below.

<樹脂成分の重量平均分子量(Mw)>
測定に使用したGPC装置は、東ソー社製HLC−8121GPC/HTであり、カラムとして東ソー社製TSKgel GMHhr−H(20)HTを用い、カラム温度を140℃に設定し、溶離液として1,2,4−トリクロロベンゼンを用いる。測定試料は、1.0mg/mlの濃度に調整し、GPC装置への注入量を0.3mlとする。各分子量の検量線は、分子量既知のポリエチレン試料を用いて校正する。重量平均分子量(Mw)は、直鎖状ポリエチレン換算値として求める。
<Weight average molecular weight (Mw) of resin component>
The GPC apparatus used for the measurement was HLC-8121GPC / HT manufactured by Tosoh Corporation, TSKgel GMHhr-H (20) HT manufactured by Tosoh Corporation was used as the column, the column temperature was set to 140 ° C., and 1,2 as the eluent. , 4-trichlorobenzene is used. The measurement sample is adjusted to a concentration of 1.0 mg / ml, and the amount injected into the GPC device is 0.3 ml. The calibration curve for each molecular weight is calibrated using a polyethylene sample with a known molecular weight. A weight average molecular weight (Mw) is calculated | required as a linear polyethylene conversion value.

<樹脂粒子、発泡性樹脂粒子及び予備発泡粒子の平均粒子径>
試料の平均粒子径は、JIS標準ふるい目開き5.60mm、4.75mm、4.00mm、3.35mm、2.80mm、2.36mm、2.00mm、1.70mm、1.40mm、1.18mm、1.00mm、0.85mm、0.71mm、0.60mm、0.50mmの篩いで分級して累積重量分布曲線を求めることにより算出する。本発明において、平均粒子径とは、累積重量分布曲線における重量50%時の粒子径を意味する。
<Average particle diameter of resin particles, expandable resin particles and pre-expanded particles>
The average particle diameter of the sample is JIS standard sieve opening 5.60mm, 4.75mm, 4.00mm, 3.35mm, 2.80mm, 2.36mm, 2.00mm, 1.70mm, 1.40mm, 1. It is calculated by classifying with a sieve of 18 mm, 1.00 mm, 0.85 mm, 0.71 mm, 0.60 mm, 0.50 mm and obtaining a cumulative weight distribution curve. In the present invention, the average particle size means a particle size at a weight of 50% in the cumulative weight distribution curve.

<発泡性樹脂粒子の発泡剤含有量>
発泡性樹脂粒子を5〜20mg精秤し、測定試料とする。この測定試料を180〜200℃に保持された熱分解炉(島津製作所社製、製品名「PYR−1A」)にセットし、測定試料を密閉後、120秒間に亘って加熱して発泡剤成分を放出させる。この放出された発泡剤成分をガスクロマトグラフ(島津製作所社製、製品名「GC−14B」、検出器:FID)を用いて下記条件にて発泡剤成分のチャートを得る。予め測定しておいた発泡剤成分の検量線に基づいて、得られたチャートから発泡性樹脂粒子中の発泡剤含有量(質量部)を算出する。
<Foaming agent content of expandable resin particles>
Weigh accurately 5 to 20 mg of the expandable resin particles to obtain a measurement sample. This measurement sample is set in a thermal decomposition furnace (manufactured by Shimadzu Corporation, product name “PYR-1A”) maintained at 180 to 200 ° C., and the measurement sample is sealed and heated for 120 seconds to be a blowing agent component. To release. A chart of the blowing agent component is obtained under the following conditions using a gas chromatograph (manufactured by Shimadzu Corporation, product name “GC-14B”, detector: FID) for the released blowing agent component. Based on the calibration curve of the foaming agent component measured in advance, the foaming agent content (parts by mass) in the foamable resin particles is calculated from the obtained chart.

ガスクロマトグラフの測定条件
カラム:信和化工社製「Shimalite 60/80 NAW」(φ3mm×3m)カラム温度:70℃
検出器温度:110℃
注入口温度:110℃
キャリアーガス:窒素
キャリアーガス流量:60ml/分
Gas chromatograph measurement conditions Column: “Shimalite 60/80 NAW” (φ3 mm × 3 m) manufactured by Shinwa Kako Co., Ltd. Column temperature: 70 ° C.
Detector temperature: 110 ° C
Inlet temperature: 110 ° C
Carrier gas: Nitrogen carrier gas Flow rate: 60 ml / min

<予備発泡粒子の嵩倍数>
約5gの予備発泡粒子の重量(a)を小数以下2位で秤量する。次に、最小メモリ単位が5cm3である500cm3メスシリンダーに秤量した予備発泡粒子を入れ、これにメスシリンダーの口径よりやや小さい円形の樹脂板であって、その中心に幅約1.5cm、長さ約30cmの棒状の樹脂板が直立して固定された押圧具を当てて、予備発泡粒子の体積(b)を読み取り、式(a)/(b)により予備発泡粒子の嵩密度(g/cm3)を求める。なお、嵩倍数は、嵩密度の逆数、即ち、式(b)/(a)とする。
<Bulk multiple of pre-expanded particles>
The weight (a) of about 5 g of pre-expanded particles is weighed at the second decimal place. Next, weighed pre-expanded particles in a 500 cm 3 graduated cylinder with a minimum memory unit of 5 cm 3 , and this is a round resin plate slightly smaller than the caliber of the graduated cylinder, with a width of about 1.5 cm at the center, The volume (b) of the pre-expanded particles is read by applying a pressing tool in which a rod-shaped resin plate having a length of about 30 cm is fixed upright, and the bulk density of the pre-expanded particles (g) / Cm 3 ). The bulk multiple is the reciprocal of the bulk density, that is, the formula (b) / (a).

<発泡成形体の倍数>
発泡成形体(成形後、50℃で4時間以上乾燥させたもの)から切り出した試験片(例75×300×35mm)の重量(a)と体積(b)をそれぞれ有効数字3桁以上になるように測定し、式(a)/(b)により発泡成形体の密度(g/cm3)を求める。なお、倍数は密度の逆数、すなわち式(b)/(a)とする。
<Multiple of foam molding>
The weight (a) and volume (b) of the test piece (example 75 × 300 × 35 mm) cut out from the foamed molded product (after being molded and dried at 50 ° C. for 4 hours or more) are each three or more significant figures. Then, the density (g / cm 3 ) of the foamed molded product is obtained by the formula (a) / (b). The multiple is the reciprocal of the density, that is, the formula (b) / (a).

<発泡成形体の引張強度>
万能試験機(オリエンテック社製、製品名「テンシロン UCT−10T」)に1000Nのロードセルを接続し、コの字型冶具で箱の長手面を挟んで500mm/分の速度で引張試験測定を行い、2次最大点荷重値を引張強度とする。
<Tensile strength of foam molding>
A 1000N load cell is connected to a universal testing machine (product name “Tensilon UCT-10T” manufactured by Orientec Co., Ltd.), and a tensile test measurement is performed at a speed of 500 mm / min. The secondary maximum point load value is taken as the tensile strength.

本発明においては、
(1)引張強度が140〜300Nである場合・・・合格(○)
(2)引張強度が140N未満である場合・・・不合格(×)
と判定する。
In the present invention,
(1) When the tensile strength is 140 to 300 N: Pass (○)
(2) When the tensile strength is less than 140 N: Fail (×)
Is determined.

<発泡成形体の割れ率>
実施例1及び比較例3で得られた箱を10箱用意し、それぞれに水10kgを入れた。箱の長手面を引っ張って50cm動かした時に割れた箱の個数を数え、下記式により割れ率を算出した。結果を表1に示す。
割れ率(%)=割れた個数×100/10
<Crack ratio of foamed molded product>
Ten boxes obtained in Example 1 and Comparative Example 3 were prepared, and 10 kg of water was added to each box. The number of boxes that were broken when the box was moved 50 cm by pulling the long side of the box was counted, and the cracking rate was calculated by the following formula. The results are shown in Table 1.
Cracking rate (%) = number of cracks × 100/10

本発明においては、
(1)割れ率が0〜20%である場合・・・・・合格(○)
(2)割れ率が20%より高い場合・・・不合格(×)
と判定する。
In the present invention,
(1) When the crack rate is 0 to 20%: Pass (○)
(2) When the cracking rate is higher than 20%: rejected (x)
Is determined.

製造例1
5リットルのオートクレーブにスチレン単量体100質量部、水100質量部、リン酸三カルシウム0.125質量部、ドデシルベンゼンスルホン酸ソーダ0.005質量部、ベンゾイルパーオキサイド0.25質量部、t−ブチルパーオキシベンゾエート0.1質量部、ジイソブチルアジペート1.0質量部を仕込み、90℃で5時間重合させた。その後、リン酸三カルシウム0.1質量部を添加し、シクロヘキサン0.7質量部、ノルマルブタン9.0質量部を圧入して110℃にて5時間保った。冷却後、水を分離し、乾燥して発泡性ポリスチレン系樹脂粒子を得た。次に、得られた発泡性ポリスチレン系樹脂粒子の表面に、表面処理剤としてステアリン酸亜鉛0.1質量%、ヒドロキシステアリン酸トリグリセライド0.08質量%を被覆し、被覆された発泡性ポリスチレン系樹脂粒子(発泡性樹脂粒子)を得た。
Production Example 1
In a 5 liter autoclave, 100 parts by mass of styrene monomer, 100 parts by mass of water, 0.125 part by mass of tricalcium phosphate, 0.005 part by mass of sodium dodecylbenzenesulfonate, 0.25 part by mass of benzoyl peroxide, t- 0.1 part by mass of butyl peroxybenzoate and 1.0 part by mass of diisobutyl adipate were charged and polymerized at 90 ° C. for 5 hours. Thereafter, 0.1 part by mass of tricalcium phosphate was added, and 0.7 part by mass of cyclohexane and 9.0 parts by mass of normal butane were injected and kept at 110 ° C. for 5 hours. After cooling, water was separated and dried to obtain expandable polystyrene resin particles. Next, 0.1% by mass of zinc stearate and 0.08% by mass of hydroxystearic acid triglyceride as a surface treatment agent are coated on the surface of the obtained expandable polystyrene resin particles. Particles (expandable resin particles) were obtained.

実施例1
(予備発泡)
製造例1で得られた被覆された発泡性ポリスチレン系樹脂粒子を、容量25Lの予備発泡装置にて予備発泡した後に20℃で24時間熟成し、嵩倍数が57倍と65倍の予備発泡粒子(第1予備発泡粒子及び第2予備発泡粒子)を得た。
嵩倍数57倍を得る時は、予備発泡装置への発泡性ポリスチレン系樹脂粒子の投入量を440g、嵩倍数65倍を得る時は発泡性ポリスチレン系樹脂粒子の投入量を385gとして予備発泡粒子を得た。
Example 1
(Pre-foaming)
The coated expandable polystyrene resin particles obtained in Production Example 1 were prefoamed in a prefoaming apparatus having a capacity of 25 L, and then aged at 20 ° C. for 24 hours to obtain prefoamed particles having a bulk ratio of 57 times and 65 times. (First pre-expanded particles and second pre-expanded particles) were obtained.
When obtaining the bulk multiple of 57 times, the amount of expandable polystyrene resin particles charged into the pre-foaming device is 440 g, and when the bulk multiple of 65 times is obtained, the amount of expandable polystyrene resin particles charged is 385 g, Obtained.

(予備発泡粒子の混合)
300×300×400mmの網籠に嵩倍数57倍の第1予備発泡粒子4600ml(100質量部)と、嵩倍数が65倍の第2予備発泡粒子12000ml(230質量部)を入れた後、同サイズの網籠を上に乗せて封をし、下方から送風機(高木鉄工所社製、製品名「電動送排風機 汎用エース型」 最大風量13m3/分)からの風を2分間当てて、網籠内で予備発泡粒子の混合物を混合した。
(Mixing of pre-expanded particles)
After putting 4600 ml (100 parts by mass) of the first pre-expanded particles having a bulk ratio of 57 times and 12000 ml (230 parts by mass) of the second pre-expanded particles having a bulk ratio of 65 times in a 300 × 300 × 400 mm screen, the same Put the size net on the top, seal it, and hit the wind from the blower (from Takagi Iron Works Co., Ltd., product name “Electric air exhaust fan general purpose ace type, maximum air flow 13m 3 / min) from the bottom for 2 minutes, A mixture of pre-expanded particles was mixed in the net.

(成形)
320mm×540mm×170mmの箱形状のキャビティを有する成形型を備えた発泡ビーズ自動成形機(積水工機製作所社製、製品名「エース11型」)のキャビティ内に前記混合物を充填し、ゲージ圧0.070MPaの水蒸気で15秒間加熱成形を行った。次に、前記金型のキャビティ内の発泡成形体を12秒間水冷した後、減圧下にて放冷して、肉厚20mmの発泡成形体を得た。
発泡成形体の割れ率は0%であった。
(Molding)
The mixture is filled in the cavity of an automatic foam bead molding machine (manufactured by Sekisui Koki Co., Ltd., product name “ACE 11 type”) having a mold having a box-shaped cavity of 320 mm × 540 mm × 170 mm, and gauge pressure Heat molding was performed for 15 seconds with water vapor of 0.070 MPa. Next, the foamed molded product in the cavity of the mold was water-cooled for 12 seconds and then allowed to cool under reduced pressure to obtain a foamed molded product having a thickness of 20 mm.
The cracking rate of the foamed molded product was 0%.

実施例2
第1予備発泡粒子を嵩倍数55倍(予備発泡装置への樹脂粒子投入量455g)とした以外は実施例1と同様にして発泡成形体を得た。
Example 2
A foamed molded article was obtained in the same manner as in Example 1 except that the first pre-expanded particles were made to have a bulk multiple of 55 times (the amount of resin particles charged into the pre-expanding apparatus was 455 g).

実施例3
第1予備発泡粒子を嵩倍数50倍(予備発泡装置への樹脂粒子投入量500g)とした以外は実施例1と同様にして発泡成形体を得た。
Example 3
A foamed molded article was obtained in the same manner as in Example 1 except that the first pre-expanded particles were 50 times in bulk (the amount of resin particles charged into the pre-expanding apparatus was 500 g).

実施例4
第2予備発泡粒子を嵩倍数70倍(予備発泡装置への樹脂粒子投入量357g)とした以外は実施例3と同様にして発泡成形体を得た。
Example 4
A foamed molded article was obtained in the same manner as in Example 3, except that the second pre-expanded particles were 70 times in bulk (the amount of resin particles charged into the pre-expanding device was 357 g).

比較例1
第1予備発泡粒子を嵩倍数62倍(予備発泡装置への樹脂粒子投入量403g)とした以外は実施例1と同様にして発泡成形体を得た。
Comparative Example 1
A foam-molded article was obtained in the same manner as in Example 1 except that the first pre-expanded particles were 62 times the bulk magnification (the amount of resin particles charged into the pre-expanding apparatus was 403 g).

比較例2
第1予備発泡粒子を嵩倍数40倍(予備発泡装置への樹脂粒子投入量625g)とし、第2予備発泡粒子を嵩倍数80倍(予備発泡装置への樹脂粒子投入量313g)とした以外は実施例1と同様にして発泡成形体を得た。
Comparative Example 2
Except for the first pre-expanded particle having a bulk multiple of 40 times (resin particle input amount to the pre-expanding device 625 g) and the second pre-expanded particle having a bulk factor 80 times (resin particle input amount to the pre-expanding device 313 g). A foamed molded product was obtained in the same manner as in Example 1.

比較例3
第1予備発泡粒子を嵩倍数60倍(予備発泡装置への樹脂粒子投入量417g)とし、第2予備発泡粒子を使用しなかったこと以外は実施例1と同様にして発泡成形体を得た。
Comparative Example 3
The first pre-expanded particles were 60 times in bulk (the amount of resin particles charged into the pre-expanding apparatus was 417 g), and a foamed molded article was obtained in the same manner as in Example 1 except that the second pre-expanded particles were not used. .

表1に実施例及び比較例の評価結果を記載する。   Table 1 shows the evaluation results of Examples and Comparative Examples.

Figure 2012207165
Figure 2012207165

表1より、実施例については発泡成形体の倍数、引張強度及び割れ率が良好な結果を示した。他方、比較例についてはこれらが良好な結果を示さない場合があった。   From Table 1, about the Example, the multiple of the foaming molded object, the tensile strength, and the crack rate showed the favorable result. On the other hand, there were cases where these did not show good results for the comparative examples.

従って、本発明によれば、高倍数で、強度に優れた発泡成形体の簡便な製造方法を提供できる。このため、本発明の発泡成形体は、包装用緩衝材、建築用部材、自動車部材等として幅広く使用することができ、特に発泡体製容器として使用できる。   Therefore, according to the present invention, it is possible to provide a simple method for producing a foamed molded article having a high multiple and excellent strength. For this reason, the foaming molding of this invention can be widely used as a cushioning material for packaging, a member for construction, an automobile member, etc., and can be used especially as a container made from a foam.

Claims (4)

嵩倍数の異なる少なくとも2種の予備発泡粒子の混合物を発泡成形することにより得られ、前記混合物が30〜80倍の第1の嵩倍数(X)を有する第1予備発泡粒子とX+5〜X+30倍の第2の嵩倍数を有する第2予備発泡粒子とを少なくとも含むことを特徴とする発泡成形体の製造方法。   A first pre-expanded particle obtained by foam-molding a mixture of at least two types of pre-expanded particles having different bulk multiples, wherein the mixture has a first bulk multiple (X) of 30 to 80 times and X + 5 to X + 30 times. And a second pre-expanded particle having the second bulk multiple. 前記発泡成形体が、樹脂成分としてポリスチレン系樹脂を含む請求項1に記載の発泡成形体の製造方法。   The manufacturing method of the foaming molding of Claim 1 in which the said foaming molding contains a polystyrene-type resin as a resin component. 請求項1又は2に記載の製造方法によって得られる発泡成形体。   The foaming molding obtained by the manufacturing method of Claim 1 or 2. 前記発泡成形体が、箱形状である請求項3に記載の発泡成形体。   The foamed molded product according to claim 3, wherein the foamed molded product has a box shape.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58215326A (en) * 1982-06-09 1983-12-14 Japan Styrene Paper Co Ltd Manufacture of polyolefin resin molding foamed in force
JPS62227631A (en) * 1986-03-29 1987-10-06 Kanegafuchi Chem Ind Co Ltd Manufacture of beads method polystyrene in-mold foam molded body
JPH06155605A (en) * 1992-11-19 1994-06-03 Iwakura Kagaku Kogyo Kk Manufacture of thermoplastic form board having internal void

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58215326A (en) * 1982-06-09 1983-12-14 Japan Styrene Paper Co Ltd Manufacture of polyolefin resin molding foamed in force
JPS62227631A (en) * 1986-03-29 1987-10-06 Kanegafuchi Chem Ind Co Ltd Manufacture of beads method polystyrene in-mold foam molded body
JPH06155605A (en) * 1992-11-19 1994-06-03 Iwakura Kagaku Kogyo Kk Manufacture of thermoplastic form board having internal void

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