JPH0657029A - Styrenic resin foam - Google Patents

Styrenic resin foam

Info

Publication number
JPH0657029A
JPH0657029A JP21126392A JP21126392A JPH0657029A JP H0657029 A JPH0657029 A JP H0657029A JP 21126392 A JP21126392 A JP 21126392A JP 21126392 A JP21126392 A JP 21126392A JP H0657029 A JPH0657029 A JP H0657029A
Authority
JP
Japan
Prior art keywords
styrene
resin
foam
resin foam
strength
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.)
Withdrawn
Application number
JP21126392A
Other languages
Japanese (ja)
Inventor
Kazuhiko Sho
和彦 正
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
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP21126392A priority Critical patent/JPH0657029A/en
Publication of JPH0657029A publication Critical patent/JPH0657029A/en
Withdrawn legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To provide a styrenic resin foam excellent in secondary expansion moldability and strength of moldings. CONSTITUTION:The styrenic resin foam is characterized by comprising a styrenic resin containing a terpenic resin. Furthermore, the styrenic resin foam in a sheetlike form has 0.1-10mm thickness and 0.03-0.5g/cc density.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は加熱二次発泡成形性に優
れ、発泡成形品の強度に優れたスチレン系樹脂発泡体に
関するものである。更に詳しくは、本発明はスチレン系
樹脂中にテルペン系樹脂を含有するスチレン系樹脂を発
泡して特定の厚み、密度を有する加熱二次発泡成形性、
成形品の強度に優れたスチレン系樹脂発泡体に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a styrenic resin foam which is excellent in secondary molding by heating and excellent in the strength of a foam molded article. More specifically, the present invention foams a styrene-based resin containing a terpene-based resin in a styrene-based resin to have a specific thickness and heat secondary foaming moldability having a specific density,
The present invention relates to a styrene resin foam having excellent strength of a molded product.

【0002】[0002]

【従来の技術】ポリスチレン系樹脂発泡体は、加熱によ
り二次発泡し、容易に所望の形状に成形でき、かつ、得
られた成形体は軽量で、機械的強度に優れ、外観が美し
く、疎水性に富み、断熱性に優れているため、箱、トレ
ー、カップ等食品包装材や簡易容器に使用されている。
最近、二次成形時の生産性向上、成形不良の減少、深絞
り性向上の観点から、二次発泡成形性の良好な、そし
て、可能な限り低温で成形できるスチレン系樹脂発泡体
が望まれている。
2. Description of the Related Art Polystyrene-based resin foam is secondary foamed by heating and can be easily molded into a desired shape, and the resulting molded body is lightweight, has excellent mechanical strength, has a beautiful appearance and is hydrophobic. It is used for food packaging materials such as boxes, trays and cups, and simple containers because of its excellent properties and excellent heat insulation.
Recently, from the viewpoint of improving productivity during secondary molding, reducing molding defects, and improving deep drawability, a styrenic resin foam having good secondary foam moldability and capable of molding at a temperature as low as possible is desired. ing.

【0003】又、食品包装用トレー等では、自動包装す
る時に割れ等が生じないよう、発泡成形品の強度向上が
求められている。
Further, in food packaging trays and the like, it is required to improve the strength of foam-molded products so that cracks and the like do not occur during automatic packaging.

【0004】[0004]

【発明が解決しようとする課題】シート状のポリスチレ
ン系発泡体を加熱炉で加熱処理して発泡させ、ついで加
熱炉から取り出して金型で成形する一連の加熱二次発泡
成形体の製造に於いて、加熱炉内の温度が不均一である
ことや外気温による炉内温度の変動の為に、シートの一
部、又は全部が加熱不足となり、成形時にシートが破れ
たり、型決まり性が悪くなったり、逆に加熱過剰となっ
て、成形品表面にケロイド状が発生したり、成形品の厚
さが変動する等の現象が生じる。
In the production of a series of heated secondary foam moldings, a sheet-shaped polystyrene foam is heat-treated in a heating furnace to be foamed, then taken out from the heating furnace and molded in a mold. However, because the temperature inside the heating furnace is not uniform or the temperature inside the furnace fluctuates due to outside air temperature, some or all of the sheets become insufficiently heated, causing the sheets to rupture during molding and the mold deciding ability to deteriorate. On the other hand, excessive heating causes conversely keloids on the surface of the molded product, fluctuations in the thickness of the molded product, and the like.

【0005】ケロイド状の発生を防ぐために、スチレン
系発泡体基材の分子量を上げたり、シート表面にフィル
ムを貼ったり、樹脂密度の大きい層、いわゆるスキン層
を形成したりする方法が知られているが、かかる方法で
は型決まり性の良い発泡体が得られにくく、深絞り成形
品の場合には、シート破れが生じやすい。又、型決まり
の良い発泡体を得る為に、スチレン系発泡体基材に可塑
剤、滑剤等を添加する方法が知られているが、二次成形
時の加熱過剰時に発生するケロイド状の不良現象が起こ
りやすい。
In order to prevent the formation of keloids, there are known methods in which the molecular weight of the styrene foam base material is increased, a film is stuck on the sheet surface, or a layer having a high resin density, that is, a skin layer is formed. However, with such a method, it is difficult to obtain a foam having good moldability, and in the case of a deep-drawing molded product, sheet breakage easily occurs. In addition, a method of adding a plasticizer, a lubricant, etc. to a styrene-based foam base material is known in order to obtain a well-defined foam, but a keloid-like defect that occurs when overheating during secondary molding is known. Phenomena are likely to occur.

【0006】ケロイド状の発生を抑え、型決まり性の良
好なスチレン系発泡体を得る方法として、分子量分布の
広いスチレン系樹脂発泡体を使用することが有効である
ことが特開昭62−22834号公報に記載されてい
る。しかし、かかる分子量分布の広いポリスチレン系樹
脂発泡体の成形品は本質的に強度が弱いという欠点を有
している。
It is effective to use a styrene-based resin foam having a wide molecular weight distribution as a method for obtaining a styrene-based foam having a good patterning property while suppressing the formation of keloids. It is described in Japanese Patent Publication No. However, such a molded product of a polystyrene resin foam having a wide molecular weight distribution has a drawback that the strength is essentially weak.

【0007】以上のごとく市場の要求を全て満足させる
発泡体は無い状況である。
As described above, there is no foam that satisfies all the requirements of the market.

【0008】[0008]

【課題を解決する為の手段】本発明者はかかる現状を鑑
み、鋭意検討を重ねた結果、スチレン系樹脂中にテルペ
ン系樹脂を含有したスチレン系樹脂より、二次加熱成形
性、ケロイド状の発生を抑え、型決まり性が良好であ
り、かつ、発泡成形品の強度が優れたスチレン系樹脂発
泡体を得ることを見出し本発明に到達した。
Means for Solving the Problems In view of the present situation, the present inventor has conducted diligent studies, and as a result, the styrene-based resin containing a terpene-based resin in the styrene-based resin has a secondary heat moldability and a keloid-like shape. The present invention has been accomplished by finding that a styrenic resin foam which suppresses the generation, has good moldability, and has excellent strength of a foam-molded article can be obtained.

【0009】すなわち、本発明は、スチレン系樹脂とテ
ルペン系樹脂とからなることを特徴とするスチレン系樹
脂発泡体であり、さらに、発泡体の厚さが0.1mm〜
10mm、密度が0.03〜0.5g/ccのシート状
であるスチレン系樹脂発泡体である。
That is, the present invention is a styrene resin foam comprising a styrene resin and a terpene resin, and the foam has a thickness of 0.1 mm to
It is a sheet-shaped styrene resin foam having a diameter of 10 mm and a density of 0.03 to 0.5 g / cc.

【0010】以下、本発明を詳細に説明する。本発明で
言うスチレン系樹脂とは、スチレン、p−メチルスチレ
ン、p−t−ブチルスチレン、α−メチルスチレン等の
スチレン系単量体単独又は混合物を重合して得られる樹
脂、スチレン系単量体と共重合可能な単量体例えば、ア
クリロニトリル、ブチルアクリレート、メチルアクリレ
ート、エチルアクリレート、メチルメタクリレート、エ
チルメタクリレート、ブチルメタクリレート、メタクリ
ル酸、アクリル酸、無水マレイン酸等とのスチレン系共
重合体樹脂、ゴム状弾性体を分散粒子として含有する上
記のスチレン系樹脂、スチレン系共重合体樹脂、及び上
記のスチレン系樹脂、スチレン系共重合体樹脂とゴム状
弾性体、例えばスチレン−ブタジエンブロック共重合体
等を混合した樹脂等である。
The present invention will be described in detail below. The styrene resin referred to in the present invention is a resin obtained by polymerizing a styrene monomer such as styrene, p-methylstyrene, pt-butylstyrene, or α-methylstyrene, or a mixture thereof, a styrene-based monomer. Monomers copolymerizable with the body, for example, acrylonitrile, butyl acrylate, methyl acrylate, ethyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate, methacrylic acid, acrylic acid, styrene copolymer resin with maleic anhydride, The above-mentioned styrene-based resin containing a rubber-like elastic material as dispersed particles, styrene-based copolymer resin, and the above-mentioned styrene-based resin, styrene-based copolymer resin and rubber-like elastic material such as styrene-butadiene block copolymer And the like are resins and the like.

【0011】スチレン系樹脂、スチレン系共重合体樹脂
の分子量は特に限定されるものではないが150000
〜500000、好ましくは180000〜45000
0、更に好ましくは200000〜400000の範囲
のスチレン系樹脂が好適に用いられる。この範囲より分
子量が小さいと、テルペン系樹脂を配合しても強度向上
の効果は小さく、この範囲より高い分子量を有するスチ
レン系樹脂、スチレン系共重合体樹脂は成形性が悪くな
り、又、スチレン系樹脂、スチレン系共重合体樹脂その
ものの生産性が低下し好ましくない。
The molecular weight of the styrene resin and the styrene copolymer resin is not particularly limited, but is 150,000.
~ 500,000, preferably 180,000-45,000
A styrene resin in the range of 0, more preferably 200,000 to 400,000 is preferably used. When the molecular weight is smaller than this range, the effect of improving the strength is small even if a terpene resin is blended, and the styrene resin and the styrene copolymer resin having a molecular weight higher than this range have poor moldability, Productivity of styrene-based resins and styrene-based copolymer resins themselves is not preferable.

【0012】テルペン系樹脂は、柑橘系皮質から得られ
るd−リモネン、又は生松脂から得られるα−ピネンの
異性化で得られるジペンテンと芳香族炭化水素をフリー
デルクラフツ型触媒(例えば塩化アルミ、三弗化硼素
等)を用いて重合を行うことにより得られる。芳香族炭
化水素としてはスチレン、α−メチルスチレン、ビニル
トルエンが好適に用いられる。
The terpene resin is a Friedel-Crafts type catalyst (for example, aluminum chloride, dipentene and aromatic hydrocarbon obtained by isomerization of d-limonene obtained from citrus cortex or α-pinene obtained from raw pine resin). It can be obtained by carrying out polymerization using boron trifluoride). Styrene, α-methylstyrene and vinyltoluene are preferably used as the aromatic hydrocarbon.

【0013】テルペン系樹脂の重合度は特に制約はない
が、重合度1000以下、好ましくは500以下、更に
好ましくは200以下である。重合度が1000を越え
るとスチレン系樹脂との相溶性が低下し、透明性が低下
するので好ましくない。テルペン系樹脂としては、例え
ば、ヤスハラケミカル株式会社のYSレジンTO−12
5,TO−115,TO−105,TO−85等が用い
ることができる。
The degree of polymerization of the terpene resin is not particularly limited, but the degree of polymerization is 1000 or less, preferably 500 or less, more preferably 200 or less. If the degree of polymerization exceeds 1000, the compatibility with the styrene resin decreases and the transparency decreases, which is not preferable. Examples of the terpene-based resin include YS resin TO-12 manufactured by Yasuhara Chemical Co., Ltd.
5, TO-115, TO-105, TO-85 and the like can be used.

【0014】テルペン系樹脂の添加方法としては、スチ
レン系単量体、あるいはスチレン系単量体と共重合可能
な単量体混合物に溶解して重合するか、スチレン系重合
体、あるいはスチレン系共重合体の重合途中にテルペン
系樹脂を溶融して、あるいは溶媒に溶解して添加する
か、重合が終了し、未反応スチレン系単量体等を除去す
る前、又は後にテルペン系樹脂を添加する等の方法を用
いることができる。
The terpene-based resin may be added by dissolving in a styrene-based monomer or a monomer mixture copolymerizable with the styrene-based monomer for polymerization, or by adding a styrene-based polymer or a styrene-based copolymer. Melt the terpene resin during the polymerization of the polymer, or add it by dissolving it in a solvent, or add the terpene resin before or after the polymerization is completed and the unreacted styrene monomer is removed. Etc. can be used.

【0015】又、スチレン系樹脂とテルペン系樹脂を混
合し、押出機あるいは成形機等で混練することも可能で
ある。スチレン系樹脂とテルペン系樹脂の混合割合は、
スチレン系樹脂100重量部当たりテルペン系樹脂0.
5〜20重量部、より好ましくは0.5〜15重量部で
ある。0.5重量部未満の場合は強度、二次成形性の向
上が認められず、20重量部を越える場合は、改良効果
が飽和し、また樹脂のコストアップを招き好ましくな
い。
It is also possible to mix a styrene resin and a terpene resin and knead them with an extruder or a molding machine. The mixing ratio of styrene resin and terpene resin is
Terpene resin per 100 parts by weight of styrene resin.
It is 5 to 20 parts by weight, more preferably 0.5 to 15 parts by weight. If it is less than 0.5 parts by weight, no improvement in strength and secondary moldability is observed, and if it exceeds 20 parts by weight, the improvement effect is saturated and the cost of the resin increases, which is not preferable.

【0016】スチレン系樹脂発泡体は、上記スチレン系
樹脂にプロパン、ブタン、ペンタン、ヘキサン等低級炭
化水素や塩化メチル、ジクロロメタン、トリクロロモノ
フルオロメタン、ジクロロジフルオロメタン等のハロゲ
ン化炭化水素等の発泡剤を含浸させて、押出機に供給す
るか、スチレン系樹脂を押出機に供給した後、押出機中
に上記発泡剤を圧入し、発泡剤とスチレン系樹脂を押出
機中で溶融、混練させ、Tダイ又はサーキュラーダイ等
から押出す等の公知の方法により、厚さが0.1〜10
mm、密度が0.03〜0.5g/ccのシート状のス
チレン系樹脂発泡体が製造される。
The styrene resin foam is a foaming agent of the above styrene resin such as lower hydrocarbons such as propane, butane, pentane and hexane, and halogenated hydrocarbons such as methyl chloride, dichloromethane, trichloromonofluoromethane and dichlorodifluoromethane. Impregnated with, and supplied to the extruder, or after supplying the styrene resin to the extruder, the foaming agent is pressed into the extruder, the foaming agent and the styrene resin are melted and kneaded in the extruder, The thickness is 0.1 to 10 by a known method such as extrusion from a T die or a circular die.
A sheet-shaped styrenic resin foam having a size of mm and a density of 0.03 to 0.5 g / cc is produced.

【0017】シートの厚さは0.1〜10mmが好まし
い。厚さが0.1mm未満であると二次発泡成形時にシ
ートが破損したり、成形品が充分な強度を有さない。ま
た、厚さが10mmを越えると二次成形が困難になるの
で好ましくない。密度は0.03〜0.5g/ccが好
ましい。密度が0.03g/cc未満であると、二次発
泡成形時にシートが破れたり、成形品強度が充分でな
く、0.5g/ccを越えると発泡品としてのメリット
が減じるため好ましくない。
The thickness of the sheet is preferably 0.1 to 10 mm. If the thickness is less than 0.1 mm, the sheet will be damaged during secondary foam molding, or the molded product will not have sufficient strength. Further, if the thickness exceeds 10 mm, secondary molding becomes difficult, which is not preferable. The density is preferably 0.03 to 0.5 g / cc. If the density is less than 0.03 g / cc, the sheet may be broken during secondary foam molding or the strength of the molded product may not be sufficient, and if it exceeds 0.5 g / cc, the merit as a foamed product may be reduced, which is not preferable.

【0018】スチレン系樹脂を発泡させ、スチレン系樹
脂発泡体を得るに当たり、発泡セル径を制御するタル
ク、炭酸カルシュウム等の造核剤、ステアリン酸、ベヘ
ニン酸、及びそれらの金属塩(カルシューム、マグネシ
ューム、亜鉛等)、エチレンビスステアロアミド等の可
塑剤、滑剤、顔料、帯電防止剤、難燃剤等を混合使用し
てもよい。また、得られたスチレン系樹脂発泡体の表面
特性を変える為に、帯電防止剤、シリコーン、抗菌剤等
の滑剤を表面に塗布してもよい。
In obtaining a styrene resin foam by foaming a styrene resin, a nucleating agent such as talc, calcium carbonate or the like, stearic acid, behenic acid, and their metal salts (calcium, magnesium) for controlling the foam cell diameter are used. , Zinc, etc.), a plasticizer such as ethylene bis-stearamide, a lubricant, a pigment, an antistatic agent, a flame retardant, etc. may be mixed and used. Further, in order to change the surface characteristics of the obtained styrene resin foam, a lubricant such as an antistatic agent, silicone or an antibacterial agent may be coated on the surface.

【0019】本発明で意図する発泡体の機能を損なわな
い範囲で、本発明で使用する特定のスチレン系樹脂に他
のスチレン系樹脂を混合して使用することも可能であ
る。以上のようにして得られたスチレン系樹脂発泡体を
加熱して二次発泡体を成形するには、スチレン系樹脂発
泡体を加熱炉に入れて、軟化、二次発泡させた後、加熱
炉から出し、直ちにプレス成形して、成形品にするのが
一般的である。
It is also possible to mix the specific styrene resin used in the present invention with another styrene resin within a range not impairing the function of the foam intended in the present invention. To mold the secondary foam by heating the styrene resin foam obtained as described above, the styrene resin foam is placed in a heating furnace, softened and secondary foamed, and then heated. It is common to take out the product and press-mold it immediately to obtain a molded product.

【0020】[0020]

【実施例】以下、実施例で更に詳しく説明する。但し、
本発明はこれらの実施例によって何ら限定されるもので
はない。 (スチレン系重合体−1の製造)撹拌機付き10リット
ルオートクレーブに、スチレン5Kg、エチルベンゼン
0.2Kg、1,1ビス(t−ブチルパーオキシ)シク
ロヘキサン1.2gを仕込み、110℃で3時間、13
0℃で3時間、150℃で2時間重合後、押出機で未反
応スチレン、エチルベンゼンを回収し、スチレン系重合
体−1を得た。GPCで測定した重量平均分子量は34
6,000であった。
EXAMPLES The present invention will be described in more detail below. However,
The invention is in no way limited by these examples. (Production of Styrene Polymer-1) A 10-liter autoclave equipped with a stirrer was charged with 5 kg of styrene, 0.2 kg of ethylbenzene and 1.2 g of 1,1 bis (t-butylperoxy) cyclohexane, and the mixture was kept at 110 ° C. for 3 hours. Thirteen
After polymerization was carried out at 0 ° C. for 3 hours and at 150 ° C. for 2 hours, unreacted styrene and ethylbenzene were recovered by an extruder to obtain a styrene polymer-1. The weight average molecular weight measured by GPC is 34.
It was 6,000.

【0021】(スチレン系重合体−2の製造)撹拌機付
き10リットルオートクレーブに、スチレン5Kg、エ
チルベンゼン0.5Kg、1,1ビス(t−ブチルパー
オキシ)シクロヘキサン1gを仕込み、120℃で2時
間、140℃で2時間、150℃で2時間重合後、押出
機で未反応スチレン、エチルベンゼンを回収し、スチレ
ン系重合体−2を得た。GPCで測定した重量平均分子
量は297,000であった。
(Production of Styrene Polymer-2) A 10 liter autoclave equipped with a stirrer was charged with 5 kg of styrene, 0.5 kg of ethylbenzene and 1 g of 1,1 bis (t-butylperoxy) cyclohexane, and the mixture was kept at 120 ° C. for 2 hours. After polymerization at 140 ° C for 2 hours and at 150 ° C for 2 hours, unreacted styrene and ethylbenzene were recovered by an extruder to obtain a styrene polymer-2. The weight average molecular weight measured by GPC was 297,000.

【0022】[0022]

【実施例1〜4】スチレン系重合体−1を100重量部
当たり、テルペン系樹脂を2,5,10,13重量部混
合し、20mm二軸押出機で造粒し、スチレン系樹脂を
得た。得られたスチレン系樹脂の物性を表1に示す。物
性の測定は以下の方法に基いて行なった。
Examples 1 to 4 2,5,10,13 parts by weight of terpene resin was mixed with 100 parts by weight of styrene polymer-1 and granulated with a 20 mm twin-screw extruder to obtain styrene resin. It was Table 1 shows the physical properties of the obtained styrene resin. The physical properties were measured according to the following methods.

【0023】(1)MFR:ISO R1133に準拠
した。 (2)VICA軟化点:ASTM D1525に準拠し
た。 (3)引張強度:ASTM D638に準拠した。 なお、用いたテルペン系樹脂はヤスハラケミカル(株)
のYSレジンTO−115である。
(1) MFR: In accordance with ISO R1133. (2) VICA softening point: According to ASTM D1525. (3) Tensile strength: According to ASTM D638. The terpene resin used is Yasuhara Chemical Co., Ltd.
YS resin TO-115.

【0024】ついで、フレオン−12を発泡剤として、
上記スチレン系樹脂を押出発泡し、厚さ1.2mm、密
度0.10g/ccのシート状のスチレン系樹脂発泡体
を得た。得られたスチレン系樹脂発泡体を1ケ月間養生
し、赤外線加熱炉を用いて種々の温度で10秒間加熱
し、二次発泡させ、図1に示す弁当箱の成形品を得た。
成形の評価結果、成形品の強度評価結果を表2に示し
た。なお、一撃衝撃強度は図1の成形品を固定し、
(a)の中心部に300gの銅球を落下させ、貫通する
高さ(cm)を測定した。
Then, Freon-12 was used as a foaming agent.
The styrene resin was extruded and foamed to obtain a sheet-shaped styrene resin foam having a thickness of 1.2 mm and a density of 0.10 g / cc. The obtained styrene-based resin foam was aged for one month, heated at various temperatures for 10 seconds using an infrared heating furnace, and secondary foamed to obtain a molded lunch box shown in FIG.
Table 2 shows the molding evaluation results and the strength evaluation results of the molded products. In addition, the impact strength is as follows:
A copper ball of 300 g was dropped on the center of (a), and the height (cm) of penetration was measured.

【0025】[0025]

【実施例5〜7】スチレン系重合体−2を用いる以外、
実施例1〜3と同様に操作し、スチレン系樹脂を得た。
物性を表1に示した。実施例1〜3と同様の操作でスチ
レン系樹脂発泡体を得、二次発泡成形を行い、弁当箱を
得た。評価結果を表2に示した。
[Examples 5 to 7] Other than using the styrene polymer-2,
The same operation as in Examples 1 to 3 was carried out to obtain a styrene resin.
The physical properties are shown in Table 1. A styrene resin foam was obtained by the same operation as in Examples 1 to 3, and secondary foam molding was performed to obtain a lunch box. The evaluation results are shown in Table 2.

【0026】[0026]

【比較例1〜2】スチレン系樹脂として、スチレン系重
合体−1〜2を用いる以外、実施例1と同様の操作を行
い、スチレン系樹脂発泡体、弁当箱を得た。スチレン系
樹脂の物性を表1に、評価結果を表2に示した。
[Comparative Examples 1 and 2] The same operation as in Example 1 was carried out except that styrene-based polymers-1 and 2 were used as the styrene-based resin to obtain a styrene-based resin foam and a lunch box. The physical properties of the styrene resin are shown in Table 1 and the evaluation results are shown in Table 2.

【0027】[0027]

【比較例3】テルペン系樹脂の変わりにミネラル・オイ
ルを2部添加する以外、実施例1と同様に操作し、スチ
レン系樹脂発泡体、弁当箱を得た。物性を表1に、評価
結果を表2に示した。
[Comparative Example 3] A styrene resin foam and a lunch box were obtained in the same manner as in Example 1 except that 2 parts of mineral oil was added instead of the terpene resin. The physical properties are shown in Table 1 and the evaluation results are shown in Table 2.

【0028】[0028]

【表1】 [Table 1]

【0029】[0029]

【表2】 [Table 2]

【0030】[0030]

【発明の効果】本発明のスチレン系樹脂発泡体は低温で
均一な軟化状態が得られる為、ケロイド状の発生のな
い、型再現性の良好な成形品が得られる。又、発泡成形
品の強度も著しく向上する。
EFFECT OF THE INVENTION Since the styrene resin foam of the present invention can obtain a uniform softened state at a low temperature, a molded product having no moldoid and good mold reproducibility can be obtained. In addition, the strength of the foam-molded product is significantly improved.

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

【図1】本発明の実施例において成形された弁当箱の概
略図である。
FIG. 1 is a schematic view of a lunch box formed in an embodiment of the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 スチレン系樹脂と、テルペン系樹脂とか
らなることを特徴とするスチレン系樹脂発泡体。
1. A styrene resin foam comprising a styrene resin and a terpene resin.
【請求項2】 発泡体の厚さが0.1mm〜10mm、
密度が0.03g/cc〜0.5g/ccのシート状で
ある請求項1記載のスチレン系樹脂発泡体。
2. The foam has a thickness of 0.1 mm to 10 mm,
The styrene-based resin foam according to claim 1, which is a sheet having a density of 0.03 g / cc to 0.5 g / cc.
JP21126392A 1992-08-07 1992-08-07 Styrenic resin foam Withdrawn JPH0657029A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21126392A JPH0657029A (en) 1992-08-07 1992-08-07 Styrenic resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21126392A JPH0657029A (en) 1992-08-07 1992-08-07 Styrenic resin foam

Publications (1)

Publication Number Publication Date
JPH0657029A true JPH0657029A (en) 1994-03-01

Family

ID=16603020

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21126392A Withdrawn JPH0657029A (en) 1992-08-07 1992-08-07 Styrenic resin foam

Country Status (1)

Country Link
JP (1) JPH0657029A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012135893A (en) * 2010-12-24 2012-07-19 Meiwa Ind Co Ltd Method for manufacturing interior trim material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012135893A (en) * 2010-12-24 2012-07-19 Meiwa Ind Co Ltd Method for manufacturing interior trim material

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