JP2008114421A - Method for producing polystyrene based resin laminated sheet - Google Patents

Method for producing polystyrene based resin laminated sheet Download PDF

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JP2008114421A
JP2008114421A JP2006298098A JP2006298098A JP2008114421A JP 2008114421 A JP2008114421 A JP 2008114421A JP 2006298098 A JP2006298098 A JP 2006298098A JP 2006298098 A JP2006298098 A JP 2006298098A JP 2008114421 A JP2008114421 A JP 2008114421A
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sheet
polystyrene
based resin
foamed
foam sheet
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Kazuyuki Ikeda
和之 池田
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Kaneka Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C66/00General aspects of processes or apparatus for joining preformed parts
    • B29C66/70General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material
    • B29C66/71General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material characterised by the composition of the plastics material of the parts to be joined

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  • Lining Or Joining Of Plastics Or The Like (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a polystyrene based resin laminated sheet which is light in weight and high in heat insulation and strength and prevents the occurrence of defective adhesion called a blister formed by the remaining of a foaming agent in the interface part between a foamed polystyrene based resin sheet and a non-foamed film and the expansion and peeling form the interface part of the foaming agent by heating during thermoforming without spoiling the characteristics excellent in appearance and designability inherent for a polystyrene based resin laminated sheet. <P>SOLUTION: After heating is carried out in advance to adjust the temperature of the lamination surface of the foamed polystyrene based resin sheet to be 50°C or higher and below 70°C, the non-foamed film is laminated on the sheet to produce the polystyrene based resin laminated sheet. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、ポリスチレン系樹脂積層シートの製造方法に関し、さらに詳しくは、ポリスチレン系樹脂発泡シートに非発泡フィルムを積層してなるポリスチレン系樹脂積層シートを製造する方法に関する。   The present invention relates to a method for producing a polystyrene resin laminated sheet, and more particularly to a method for producing a polystyrene resin laminated sheet obtained by laminating a non-foamed film on a polystyrene resin foam sheet.

ポリスチレン系樹脂発泡シートは成形性に優れ、断熱性が高く、軽量で外観美麗な容器を容易に得ることができるため、食品包装容器の材料として広く用いられている。更にポリスチレン系樹脂発泡シートに非発泡ポリスチレン樹脂を積層したポリスチレン系樹脂積層シートは強度や外観美麗性に優れており、その利点をいかし、即席麺等の食品容器として、数多く使用されている。しかし最近ではリサイクル法施行に伴い発泡シート層の軽量化が一段と進み、成形の難度が著しく上がり、その結果、成形容器の強度低下の問題を生じている。このため高強度化のための方策として、押出発泡成形時に表面を冷却してポリスチレン系樹脂発泡シートの表層部を高密度化することに加えて残存発泡剤量を2.3〜3.0重量%にすることが提案されている(例えば特許文献1)。   Polystyrene resin foam sheets are widely used as materials for food packaging containers because they are excellent in moldability, have high heat insulation properties, and can easily obtain lightweight and beautiful containers. Furthermore, a polystyrene-based resin laminated sheet obtained by laminating a non-expanded polystyrene resin on a polystyrene-based resin foamed sheet is excellent in strength and appearance, and is used in many cases as a food container such as instant noodles. However, recently, with the enforcement of the recycling law, the weight reduction of the foamed sheet layer has further progressed, and the difficulty of molding has increased remarkably, resulting in a problem of reduced strength of the molded container. For this reason, as a measure for increasing the strength, the surface is cooled during extrusion foaming to increase the density of the surface layer portion of the polystyrene resin foam sheet, and the amount of the remaining foaming agent is 2.3 to 3.0 weight. % Is proposed (for example, Patent Document 1).

しかし、残存発泡剤量を高くするということは発泡シート中の発泡剤量を熱成形に適した量まで低下させるための養生期間が長くなることを意味する。十分な養生を行なう前にポリスチレン系樹脂発泡シートをTダイを備えた押出機より溶融状態の非発泡ポリスチレン樹脂を加熱ロール等を介し熱融着すると、ポリスチレン系樹脂発泡シートと非発泡フィルムを均一に圧着することができず、ポリスチレン系樹脂発泡シートと非発泡フィルムの界面部分に接着不良部分が生じる。やがてその部分に発泡剤が滞留し、熱成形時の加熱により界面より剥離膨張し、火膨れと呼ばれる外観不良が発生し商品として通用しないものとなってしまう。このため発泡シート中の発泡剤量が加熱成形に適正な量まで低下するまで長期間在庫しておかなくてはならず、保管にかかるコストのために成形品がコスト高となるという新たな問題が発生した。これらの現象は冬場において特に大きな問題となっている。
従って、ポリスチレン系樹脂積層シートの製造に当たってコストダウンの観点から、ポリスチレン系樹脂発泡シートの養生期間を短縮するため、様々な取り組みが行われてきた。
However, increasing the amount of residual foaming agent means that the curing period for reducing the amount of foaming agent in the foamed sheet to an amount suitable for thermoforming becomes longer. Prior to sufficient curing, a polystyrene resin foam sheet and a non-foamed film are made uniform by thermally fusing a non-foamed polystyrene resin in a molten state through a heating roll from an extruder equipped with a T-die. Cannot be pressure-bonded to each other, and a poorly bonded portion is generated at the interface portion between the polystyrene resin foam sheet and the non-foamed film. Eventually, the foaming agent stays in the part, and peeling and expansion occurs from the interface due to heating at the time of thermoforming, and an appearance defect called blistering occurs, which makes it unusable as a product. For this reason, it must be stocked for a long time until the amount of the foaming agent in the foamed sheet is reduced to an appropriate amount for thermoforming, and a new problem that the cost of the molded product is high due to the cost of storage. There has occurred. These phenomena are particularly serious problems in winter.
Therefore, various efforts have been made to shorten the curing period of the polystyrene resin foam sheet from the viewpoint of cost reduction in the production of the polystyrene resin laminate sheet.

例えば発泡シートを製造し、巻取る際、巻取りの張力を弱めることにより、ロール巻されたシートの間隔を広げ、空気の流入効率を向上させ、養生期間の短縮を図る方法(例えば特許文献2)が提案されている。しかし、巻取り張力を低下すると、工程内でシートが蛇行したり、ロール巻されたシートの取り扱いが極端に悪くなる等の問題が生じ、生産性の悪化につながる場合がある。   For example, when a foamed sheet is manufactured and wound, a method of increasing the interval between the rolled sheets by increasing the winding tension, improving the air inflow efficiency, and shortening the curing period (for example, Patent Document 2) ) Has been proposed. However, when the winding tension is lowered, problems such as the meandering of the sheet in the process and the handling of the roll-wound sheet become extremely bad may occur, leading to deterioration of productivity.

また、ブタン以上の透過係数を有するプロパンを物理発泡剤としてブタンと併用する方法や(例えば特許文献3)、空気の5倍以上の透過係数を有する炭酸ガス、水、沸点140℃以下のエーテル、沸点140以下のジアルキルカーボネートのいずれかを1種類以上を物理発泡剤としてブタン等と併用する方法も提案されている(例えば特許文献4)。しかし、これらの方法は、発泡シート全体の残存発泡剤量を減少させることにのみ着目したものであり、この方法では残存発泡剤量が少ない為、軽量化に係るシートにおいては高強度化を達成することができない。
特開2005−319764 特開平9−48030 特開2001−105471 特開2003−231169
In addition, propane having a permeability coefficient of butane or higher is used as a physical foaming agent in combination with butane (for example, Patent Document 3), carbon dioxide gas having a permeability coefficient five times that of air, water, ether having a boiling point of 140 ° C. or lower, There has also been proposed a method in which one or more dialkyl carbonates having a boiling point of 140 or less are used in combination with butane or the like using one or more types as physical foaming agents (for example, Patent Document 4). However, these methods focus only on reducing the amount of remaining foaming agent in the entire foamed sheet, and since this method has a small amount of residual foaming agent, high strength is achieved in the sheet for weight reduction. Can not do it.
JP-A-2005-319764 JP 9-48030 A JP 2001-105471 A JP2003-231169A

本発明は、上記のような問題を解決するためのものであり、機械物性および接着性に優れたポリスチレン系樹脂積層シートを提供することを目的とする。   This invention is for solving the above problems, and it aims at providing the polystyrene-type resin laminated sheet excellent in mechanical physical property and adhesiveness.

本発明者等は、上記課題を解決すべく鋭意研究した結果、軽量でかつ高強度を目的として残存発泡剤量が高いポリスチレン系樹脂発泡シートの積層面の表面温度をある温度範囲に温調した後、非発泡フィルムを積層すると界面部分に接着不良の発生を抑止でき、残存発泡剤が高いシートにおいても安定的に良好なポリスチレン系樹脂積層シート得られることを見出し、本発明に至った。   As a result of earnest research to solve the above problems, the present inventors have adjusted the surface temperature of the laminated surface of the polystyrene-based resin foam sheet having a high amount of residual foaming agent to be lightweight and high strength within a certain temperature range. Later, when a non-foamed film was laminated, the occurrence of poor adhesion at the interface portion could be suppressed, and it was found that a good polystyrene-based resin laminated sheet could be obtained stably even in a sheet having a high residual foaming agent.

すなわち本発明は、ポリスチレン系樹脂発泡シートに非発泡フィルムを積層してなるポリスチレン系樹脂積層シートの製造方法であって、ポリスチレン系樹脂発泡シートの積層面の表面温度が50℃以上70℃未満となるように予め加熱処理を行なった後、該処理を施した面に非発泡フィルムを積層することを特徴とするポリスチレン系樹脂積層シートの製造方法である。   That is, the present invention is a method for producing a polystyrene resin laminated sheet obtained by laminating a non-foamed film on a polystyrene resin foam sheet, and the surface temperature of the laminated surface of the polystyrene resin foam sheet is 50 ° C. or higher and less than 70 ° C. After the heat treatment is performed in advance, a non-foamed film is laminated on the surface subjected to the heat treatment.

前記非発泡フィルムは、ポリスチレン系樹脂の非発泡フィルムであることが好ましく、前記ポリスチレン系樹脂発泡シートの厚みが1mm以上3mm以下であり、前記非発泡フィルムの厚みが100μm以上200μm以下であることも好ましい。   The non-foamed film is preferably a non-foamed film of polystyrene resin, the thickness of the polystyrene-based resin foam sheet is 1 mm or more and 3 mm or less, and the thickness of the non-foamed film is 100 μm or more and 200 μm or less. preferable.

本発明によって得られるポリスチレン系樹脂積層シートは、外観および成形性が優れている。   The polystyrene resin laminated sheet obtained by the present invention is excellent in appearance and moldability.

以下、本発明の実施の形態について詳細に説明する。
本発明のポリスチレン系樹脂積層シートの製造方法においては、ポリスチレン系樹脂発泡シートの積層面の表面温度を、50℃から70℃未満の温度範囲のうちのいずれかの温度になるよう加熱処理し、非発泡フィルムを積層する。本発明のポリスチレン系樹脂積層シートの製造に用いられるポリスチレン系樹脂発泡シートは、公知のいずれのポリスチレン系樹脂発泡シートでもよい。押出発泡による発泡シート製造プロセスは、広く一般に行われている方法で行うことができる。例えば、ポリスチレン系樹脂に造核剤などを混合した樹脂組成物を、押出機を用いて溶融混合し、発泡剤を圧入した後、更に、発泡に適した温度となるまで溶融樹脂を冷却して、サーキュラー・ダイより低圧域に押出し(すなわち、圧力開放による発泡を行い)、円筒状発泡体を得、円筒状発泡体の内面側から冷却するように円筒状発泡体の内側に位置して設置された円筒状冷却筒にて成形した後、切り開いて発泡シートを得られる方法が知られている。
Hereinafter, embodiments of the present invention will be described in detail.
In the method for producing a polystyrene-based resin laminate sheet of the present invention, the surface temperature of the laminate surface of the polystyrene-based resin foam sheet is heat-treated so as to be any temperature within a temperature range of 50 ° C. to less than 70 ° C., Laminate non-foamed film. Any known polystyrene resin foam sheet may be used as the polystyrene resin foam sheet used in the production of the polystyrene resin laminate sheet of the present invention. The process for producing a foam sheet by extrusion foaming can be performed by a widely used method. For example, a resin composition in which a nucleating agent is mixed with a polystyrene resin is melt-mixed using an extruder, and after the foaming agent is pressed in, the molten resin is further cooled to a temperature suitable for foaming. , Extrude into the low pressure range from the circular die (ie foaming by pressure release) to obtain a cylindrical foam, located inside the cylindrical foam to cool from the inner surface side of the cylindrical foam A method is known in which a foamed sheet can be obtained after being molded by a cylindrical cooling cylinder.

本発明で用いられる発泡剤としては、特に制限はないが例えば、プロパン、ブタン、ペンタンなどの物理発泡剤、または、重曹−クエン酸、アゾジカルボンアミド、ジニトロソペンタメチレンテトラミン、アゾビスイソブチルニトリルなどの化学発泡剤があげられる。また、工業的に入手容易なブタン系発泡剤が多用されている。なかでも、シートの熱成形性・発泡剤ガスの保持性の観点から、イソブタン70〜100重量%およびノルマルブタン0〜30重量%からなる混合ブタンを用いることが好ましい。   The blowing agent used in the present invention is not particularly limited. For example, physical blowing agents such as propane, butane, pentane, or sodium bicarbonate-citric acid, azodicarbonamide, dinitrosopentamethylenetetramine, azobisisobutylnitrile, etc. Chemical foaming agents. In addition, industrially easily available butane-based blowing agents are frequently used. Especially, it is preferable to use the mixed butane which consists of 70-100 weight% of isobutane and 0-30 weight% of normal butane from a viewpoint of the thermoformability of a sheet | seat, and the retainability of a foaming agent gas.

本発明で用いられる造核剤としては、多孔質無機粉末、例えば、炭酸カルシウム、硫酸バリウム、シリカ、酸化チタン、クレー、酸化アルミニウム、ベントナイト、ケイソウ土、タルク等が使用できる。また、必要に応じて、樹脂中の造核剤の分散をよくするために、エチレンビスステアリルアミド、ステアリン酸マグネシウム等の脂肪酸金属塩、脂肪酸エステル等の滑剤等を添加しても良い。
本発明におけるポリスチレン系樹脂発泡シートの目付量は、200g/m2以上であることが好ましい。ポリスチレン系樹脂発泡シートの目付量が200g/m2未満では、容器強度を満足する容器を得ることができない傾向がある。また、ポリスチレン系樹脂発泡シートの目付量の増加は、容器強度の向上に繋がる反面、コストアップになることから、400g/m2以下にすることが好ましい。
As the nucleating agent used in the present invention, porous inorganic powders such as calcium carbonate, barium sulfate, silica, titanium oxide, clay, aluminum oxide, bentonite, diatomaceous earth, talc and the like can be used. Further, if necessary, in order to improve dispersion of the nucleating agent in the resin, a fatty acid metal salt such as ethylene bisstearylamide and magnesium stearate, a lubricant such as a fatty acid ester, and the like may be added.
The basis weight of the polystyrene-based resin foam sheet in the present invention is preferably 200 g / m 2 or more. When the basis weight of the polystyrene resin foam sheet is less than 200 g / m 2, there is a tendency that a container satisfying the container strength cannot be obtained. In addition, an increase in the basis weight of the polystyrene resin foam sheet leads to an improvement in container strength, but increases the cost. Therefore, it is preferable to set the amount to 400 g / m 2 or less.

本発明におけるポリスチレン系樹脂発泡シートの残存発泡剤量は、主に、ポリスチレン系樹脂の押出発泡による製造時の発泡剤の圧入量、および発泡時のポリスチレン系樹脂の樹脂温度によって決まる。また、後述するポリスチレン系樹脂発泡シートの表層部の密度を上げることも、ポリスチレン系樹脂発泡シート表面からの発泡剤の散逸を抑える効果を有し、残存発泡剤量の確保に有効である。   The amount of the remaining foaming agent of the polystyrene-based resin foam sheet in the present invention is mainly determined by the amount of the foaming agent injected during the production by extrusion foaming of the polystyrene-based resin and the resin temperature of the polystyrene-based resin at the time of foaming. Further, increasing the density of the surface layer portion of the polystyrene-based resin foam sheet, which will be described later, has an effect of suppressing the dissipation of the foaming agent from the surface of the polystyrene-based resin foam sheet, and is effective in securing the amount of residual foaming agent.

ポリスチレン系樹脂発泡シートに残存発泡剤(ガス)量が多くなるにポリスチレン系樹脂発泡シートのセル内でのガス圧力が高くなり、容器強度が向上する。本発明におけるポリスチレン系樹脂発泡シートの残存発泡剤量は、十分に強度の高い容器を得るために、2.3〜3.0重量%であることが好ましく、2.5〜2.8重量%であることがより好ましい。ポリスチレン系樹脂発泡シートの残存発泡剤量が2.3重量%未満であれば、得られる容器の容器強度が低下する傾向がある。また、残存発泡剤量が3.0重量%を越える場合には、ポリスチレン系樹脂非発泡フィルムとの積層時にポリスチレン系樹脂発泡シートから発泡剤ガスが散逸して、両者の積層界面に空隙が生じ、成形の加熱時にポリスチレン系樹脂非発泡フィルムとポリスチレン系樹脂発泡シートとの界面が剥離する現象(いわゆる、火膨れ現象)を生じさせ、容器外観が大きく損なわれる傾向がある。   As the amount of the remaining foaming agent (gas) increases in the polystyrene resin foam sheet, the gas pressure in the cell of the polystyrene resin foam sheet increases, and the container strength is improved. In order to obtain a sufficiently strong container, the amount of the remaining foaming agent in the polystyrene resin foam sheet in the present invention is preferably 2.3 to 3.0% by weight, and 2.5 to 2.8% by weight. It is more preferable that If the amount of the remaining foaming agent in the polystyrene-based resin foam sheet is less than 2.3% by weight, the container strength of the resulting container tends to decrease. In addition, when the amount of the remaining foaming agent exceeds 3.0% by weight, the foaming agent gas is dissipated from the polystyrene resin foam sheet during lamination with the polystyrene resin non-foamed film, and voids are generated at the lamination interface between the two. There is a tendency that the interface between the polystyrene-based resin non-foamed film and the polystyrene-based resin foamed sheet is peeled off during heating of molding (so-called blistering phenomenon), and the container appearance is greatly impaired.

本発明におけるポリスチレン系樹脂発泡シートの独立気泡率は、ポリスチレン系樹脂積層発泡シート中の発泡剤ガスの散逸を抑え、長期間での強度物性を維持するために、85%以上が好ましく、90%以上がより好ましい。ポリスチレン系樹脂発泡シートの独立気泡率が85%未満の場合には、発泡シートの残存発泡剤の散逸が早くなり、気泡内の圧力が維持できず、強度が大幅に低下する他、成形時の加熱による二次発泡力も低下するため、良好な成形が不可能となる傾向がある。なお、ポリスチレン系樹脂発泡シートの独立気泡率は、Air Comparison Pycnometer(例えば、BECKMAN製model1930等)を用いて測定することができる。   The closed cell ratio of the polystyrene resin foam sheet in the present invention is preferably 85% or more, and 90% in order to suppress the dissipation of the foaming agent gas in the polystyrene resin laminated foam sheet and maintain the strength properties over a long period of time. The above is more preferable. When the closed cell ratio of the polystyrene resin foam sheet is less than 85%, the remaining foaming agent in the foam sheet is quickly dissipated, the pressure inside the foam cannot be maintained, and the strength is greatly reduced. Since the secondary foaming power by heating is also reduced, good molding tends to be impossible. The closed cell ratio of the polystyrene resin foam sheet can be measured using an Air Comparison Pycnometer (for example, model 1930 manufactured by BECKMAN).

本発明においては、押出発泡法にてポリスチレン系樹脂発泡シートを製造する際、ポリスチレン系樹脂発泡シート表面に空気を吹き付けて急冷することにより、ポリスチレン系樹脂発泡シートの表層部の密度を高くすることができる。目標とする表層部の密度を得るためには、押出直後のシート表面温度、押出樹脂吐出量、シート引き取り速度等に合わせて、冷却空気の温度、風量、風速および吹き付け位置を適宜調整すればよい。   In the present invention, when producing a polystyrene resin foam sheet by an extrusion foaming method, the surface layer portion of the polystyrene resin foam sheet is increased in density by blowing air onto the surface of the polystyrene resin foam sheet and rapidly cooling it. Can do. In order to obtain the target density of the surface layer portion, the temperature of the cooling air, the air volume, the wind speed, and the spraying position may be appropriately adjusted according to the sheet surface temperature immediately after extrusion, the extrusion resin discharge amount, the sheet take-up speed, etc. .

本発明のポリスチレン系樹脂積層シートの製造に用いられる非発泡フィルムは、樹脂製のフィルムであれば特に限定されない。ポリスチレン系樹脂発泡シートと同じ基材樹脂から調製されるフィルムであっても異なるフィルムであってもよいが、ポリスチレン系樹脂フィルムが好ましく用いられる。ポリスチレン系樹脂フィルムは、例えば、耐衝撃性ポリスチレン、スチレン単独重合体、p−メチルスチレン単独重合体、スチレン−無水マレイン酸共重合体、スチレン−アクリロニトリル共重合体、スチレン−アクリル酸共重合体、スチレン−メタクリル酸共重合体、スチレン−ブタジエン共重合体、スチレン−ブタジエン−アクリロニトリル共重合体、ポリスチレンとポリフェニレンオキシドとの混合物等から選択される1種類または2種類以上の組み合わせから調製され得る。   The non-foamed film used for the production of the polystyrene-based resin laminate sheet of the present invention is not particularly limited as long as it is a resin film. Although it may be a film prepared from the same base resin as the polystyrene resin foam sheet or a different film, a polystyrene resin film is preferably used. The polystyrene resin film is, for example, impact-resistant polystyrene, styrene homopolymer, p-methylstyrene homopolymer, styrene-maleic anhydride copolymer, styrene-acrylonitrile copolymer, styrene-acrylic acid copolymer, It can be prepared from one or a combination of two or more selected from styrene-methacrylic acid copolymers, styrene-butadiene copolymers, styrene-butadiene-acrylonitrile copolymers, mixtures of polystyrene and polyphenylene oxide, and the like.

非発泡フィルムの製造方法は、特に限定されないが、一般的には、押出フィルムの製造方法を用いて製造される。即ち、樹脂を押出機で溶融させ、ダイスにてフィルム状に成型して得られる。この製造方法は、サーキュラーダイを用いるインフレーション法、Tダイを用いるTダイ法が一般的であるが、数10μmの厚みのフィルムを得る為には、インフレーション法が好ましく用いられ、100μm以上の厚みのフィルムを得る為には、Tダイ法が好ましく用いられ得る。   Although the manufacturing method of a non-foamed film is not specifically limited, Generally, it manufactures using the manufacturing method of an extruded film. That is, it is obtained by melting the resin with an extruder and molding it into a film with a die. As this manufacturing method, an inflation method using a circular die and a T die method using a T die are generally used. In order to obtain a film having a thickness of several tens of μm, the inflation method is preferably used. In order to obtain a film, the T-die method can be preferably used.

本発明のポリスチレン系樹脂積層シートの製造方法における、ポリスチレン系樹脂発泡シート表面の加熱処理の手段は、特に限定されず、接触加熱処理および非接触加熱処理のいずれの手段も用いられ得る。   The means for heat treatment of the polystyrene resin foam sheet surface in the method for producing a polystyrene resin laminated sheet of the present invention is not particularly limited, and any means of contact heat treatment and non-contact heat treatment can be used.

接触加熱処理においては、加熱ロールあるいは加熱板等の高温体に、ポリスチレン系樹脂発泡シートを直接接触させる。このうち、ポリスチレン系樹脂発泡シートを加熱ロールに接触させる方法としては、限定はされないが、図1に示すように、ポリスチレン系樹脂発泡シート1を加熱ロール2の表面に巻き付けて、接触させる方法が例示される。ポリスチレン系樹脂発泡シート1と加熱ロール2との接触時間は加熱ロール2の回転速度と、接触長さを変えることで適宜調整し得る。   In the contact heat treatment, the polystyrene-based resin foam sheet is brought into direct contact with a high-temperature body such as a heating roll or a heating plate. Of these methods, the method of bringing the polystyrene resin foam sheet into contact with the heating roll is not limited, but as shown in FIG. 1, there is a method in which the polystyrene resin foam sheet 1 is wound around the surface of the heating roll 2 and brought into contact therewith. Illustrated. The contact time between the polystyrene-based resin foam sheet 1 and the heating roll 2 can be appropriately adjusted by changing the rotation speed and the contact length of the heating roll 2.

非接触加熱処理においては、熱風装置3や熱風加熱炉、赤外線ヒーターなどを用いて、ポリスチレン系樹脂発泡シートの積層面の加熱を行なう。この場合は、発泡シート内部で二次発泡が起こらないように条件を設定する必要がある。いずれの場合においても、加熱処理において、ポリスチレン系樹脂発泡シート表面の温度は、50℃以上70℃未満の温度範囲のうちの任意のいずれかの温度になるようにする。50℃より低い温度では表層部のガス拡散の効果が見られない。70℃より高い温度では、ポリスチレン系樹脂発泡シートの加熱面が二次発泡して、表面性や強度が変化し、ポリスチレン系樹脂発泡シートの変形が大きくなりすぎ、巾および厚みが成形に適正な範囲を超えてしまう。更に、加熱処理に熱ロールを用いた場合にはポリスチレン系樹脂発泡シートが熱ロールに融着し、発泡シートの走行が不可能となる。   In the non-contact heat treatment, the laminated surface of the polystyrene-based resin foam sheet is heated using a hot air device 3, a hot air heating furnace, an infrared heater, or the like. In this case, it is necessary to set conditions so that secondary foaming does not occur inside the foam sheet. In any case, in the heat treatment, the temperature of the surface of the polystyrene-based resin foam sheet is set to any one of temperatures in the temperature range of 50 ° C. or higher and lower than 70 ° C. At a temperature lower than 50 ° C., the effect of gas diffusion in the surface layer portion is not observed. At a temperature higher than 70 ° C., the heated surface of the polystyrene resin foam sheet undergoes secondary foaming, the surface properties and strength change, the deformation of the polystyrene resin foam sheet becomes excessively large, and the width and thickness are appropriate for molding. It will be out of range. Furthermore, when a heat roll is used for the heat treatment, the polystyrene-based resin foam sheet is fused to the heat roll, and the foam sheet cannot run.

こように加熱処理が施されたポリスチレン系樹脂発泡シートに、非発泡フィルムを積層する方法は特に限定されない。例えば、非発泡フィルムを押出機より押出しながら、加圧ロールで、ポリスチレン系樹脂発泡シートの加熱処理面にフィルムを積層する方法、予め別工程で製造した非発泡フィルムを、ポリスチレン系樹脂発泡シートと熱融着する方法、およびポリスチレン系樹脂発泡シートと非発泡フィルムとを接着剤により積層する方法等が挙げられる。   Thus, the method of laminating a non-foamed film on the polystyrene-based resin foam sheet subjected to the heat treatment is not particularly limited. For example, while extruding a non-foamed film from an extruder, a method of laminating a film on a heat-treated surface of a polystyrene-based resin foam sheet with a pressure roll, a non-foamed film manufactured in a separate process in advance and a polystyrene-based resin foam sheet Examples thereof include a method of heat-sealing and a method of laminating a polystyrene resin foam sheet and a non-foamed film with an adhesive.

以下に実施例を挙げて本発明を詳細に説明するが、本発明はこれらに限定されない。   Hereinafter, the present invention will be described in detail with reference to examples, but the present invention is not limited thereto.

(実施例1)ポリスチレン系樹脂発泡シートはポリスチレン樹脂(PSジャパン製、G0002)100重量部に対して、気泡調整剤であるタルク(林化成株式会社製、タルカンPK)0.3部および滑剤としてステアリン酸マグネシウム0.02重量部添加しポリスチレン系樹脂組成物とした。115−180mmφのタンデム押出機に前記ポリスチレン系樹脂組成物を投入し、設定温度200℃に加熱された一段目の押出機にて前記混合物を溶融し、発泡剤としてブタン系ガス(イソブタン85重量%/ノルマルブタン15重量%の混合物)14L/hrを圧入した後、二段目の押出機にて樹脂温度が150℃となるように冷却後、150℃に設定したサーキュラーダイより大気中に押出発泡させた。引取速度を9m/minとし、非発泡フィルムを積層しない面に対して30℃の冷風を1.5m3/min、積層する面に25℃の冷風を風を4.5m3/minの風量で吹き付け、幅1050mm、目付量250g/m2、非積層面、積層面のそれぞれの表層部密度を0.25g/cm3、0.45g/cm3、独立気泡率90%のポリスチレン系押出発泡シートを得た。得られた発泡シートは25℃の温度で20日間養生した。 (Example 1) Polystyrene-based resin foam sheet is 100 parts by weight of polystyrene resin (manufactured by PS Japan, G0002), 0.3 parts of talc (manufactured by Hayashi Kasei Co., Ltd., Talkan PK) as a foam regulator, and as a lubricant. 0.02 part by weight of magnesium stearate was added to make a polystyrene resin composition. The polystyrene-based resin composition is charged into a 115-180 mmφ tandem extruder, and the mixture is melted in a first-stage extruder heated to a preset temperature of 200 ° C., and a butane-based gas (isobutane 85 wt% as a blowing agent). / 15% by weight mixture of normal butane) 14L / hr was injected and cooled with a second stage extruder so that the resin temperature would be 150 ° C, then extruded and foamed into the atmosphere from a circular die set at 150 ° C. I let you. The take-off rate was 9m / min, non-foamed film 30 ° C. of the cold air of 1.5 m 3 / min to a plane without stacking, the cold air of 25 ° C. to laminated surfaces in air volume of 4.5 m 3 / min of air spraying, width 1050 mm, basis weight 250 g / m 2, non-laminated surface, each surface portion density 0.25 g / cm 3 of the laminate surface, 0.45 g / cm 3, closed cell content of 90% polystyrene extruded foam sheet Got. The obtained foamed sheet was cured at a temperature of 25 ° C. for 20 days.

得られたポリスチレン系樹脂発泡シートの密度0.45g/cm3 の面を、加熱ロールを用いて接触加熱処理した。すなわち、加熱ロールを60℃に加熱し、26m/分の速度で接触加熱した直後のポリスチレン系樹脂発泡シートの加熱処理面に127μmの非発泡ポリスチレン系樹脂フィルム(PSジャパン製、スタイロン475D)を押出しラミネーションにて積層した。得られたポリスチレン系樹脂積層シートは発泡シートと非発泡フィルムが均一に接着していた。 The surface of the obtained polystyrene-based resin foam sheet having a density of 0.45 g / cm 3 was subjected to contact heat treatment using a heating roll. That is, a non-foamed polystyrene resin film (PS Japan, Stylon 475D) having a thickness of 127 μm was extruded onto the heat-treated surface of the polystyrene resin foam sheet immediately after heating the heating roll to 60 ° C. and contact heating at a speed of 26 m / min. Laminated by lamination. In the obtained polystyrene resin laminated sheet, the foamed sheet and the non-foamed film were uniformly bonded.

(実施例2)加熱ロールを90℃に加熱した以外は、実施例1と同様にしてポリスチレン系樹脂積層シートを得た。得られた積層シートは発泡シートと非発泡フィルムが均一に接着していた。   (Example 2) A polystyrene-based resin laminated sheet was obtained in the same manner as in Example 1 except that the heating roll was heated to 90 ° C. In the obtained laminated sheet, the foamed sheet and the non-foamed film were uniformly bonded.

(実施例3)実施例1で得られたポリスチレン系樹脂発泡シートの密度0.45g/cm3 の面に、熱風装置の150℃の風で加熱処理を施しした以外は、実施例1と同様にしてポリスチレン系樹脂積層シートを得た。得られた積層シートは発泡シートと非発泡フィルムが均一に接着していた。 (Example 3) Similar to Example 1, except that the surface of the polystyrene resin foam sheet obtained in Example 1 having a density of 0.45 g / cm 3 was subjected to a heat treatment with a 150 ° C wind of a hot air device. Thus, a polystyrene resin laminated sheet was obtained. In the obtained laminated sheet, the foamed sheet and the non-foamed film were uniformly bonded.

(実施例4)熱風装置の風温を250℃した以外は、実施例3と同様にしてポリスチレン系樹脂積層シートを得た。得られた積層シートは発泡シートと非発泡フィルムが均一に接着していた。   (Example 4) A polystyrene-based resin laminated sheet was obtained in the same manner as in Example 3 except that the air temperature of the hot air device was 250 ° C. In the obtained laminated sheet, the foamed sheet and the non-foamed film were uniformly bonded.

(実施例5)実施例1で得られたポリスチレン系樹脂発泡シートの密度0.45g/cm3 の面に、加熱ロールを90℃に加熱した後、熱風装置の150℃の風で加熱処理を施しした以外は、実施例1と同様にしてポリスチレン系樹脂積層シートを得た。得られた積層シートは発泡シートと非発泡フィルムが均一に接着していた。 (Example 5) On the surface of the polystyrene resin foam sheet obtained in Example 1 having a density of 0.45 g / cm 3 , a heating roll was heated to 90 ° C, and then heat treatment was performed with 150 ° C wind from a hot air device. A polystyrene-based resin laminate sheet was obtained in the same manner as in Example 1 except that it was applied. In the obtained laminated sheet, the foamed sheet and the non-foamed film were uniformly bonded.

(比較例1)一切の熱処理を行なわなかった以外は実施例1と同様にしてポリスチレン系樹脂積層シートを得た。得られた積層シートは発泡シートと非発泡フィルムの界面で
火膨れが発生した。
(Comparative Example 1) A polystyrene-based resin laminated sheet was obtained in the same manner as in Example 1 except that no heat treatment was performed. In the obtained laminated sheet, blistering occurred at the interface between the foamed sheet and the non-foamed film.

(比較例2)加熱ロールを40℃に加熱した以外は、実施例1と同様にしてポリスチレン系樹脂積層シートを得た。得られた積層シートは発泡シートと非発泡フィルムの界面で火膨れが発生した。   (Comparative Example 2) A polystyrene-based resin laminated sheet was obtained in the same manner as in Example 1 except that the heating roll was heated to 40 ° C. In the obtained laminated sheet, blistering occurred at the interface between the foamed sheet and the non-foamed film.

(比較例3)加熱ロールを120℃に加熱したポリスチレン系樹脂発泡シートの積層面は過剰な熱により表層部分の表面性が変化しており、実施例1と同様にしてポリスチレン系樹脂積層シートを得た発泡シートと非発泡フィルムの界面で火膨れが発生した。   (Comparative Example 3) The surface properties of the surface layer portion of the laminated surface of the polystyrene resin foam sheet heated to 120 ° C. with the heating roll changed due to excessive heat. A blister occurred at the interface between the obtained foamed sheet and the non-foamed film.

(比較例4)実施例1で得られたポリスチレン系樹脂発泡シートの密度0.45g/cm3 の面に、熱風装置の100℃の風で加熱処理を施しした。それ以外は、実施例3と同様にしてポリスチレン系樹脂積層シートを得た。得られた積層シートは発泡シートと非発泡フィルムの界面で火膨れが発生した。 (Comparative Example 4) The surface of the polystyrene resin foam sheet obtained in Example 1 having a density of 0.45 g / cm 3 was subjected to heat treatment with 100 ° C. wind from a hot air apparatus. Other than that was carried out similarly to Example 3, and obtained the polystyrene-type resin laminated sheet. In the obtained laminated sheet, blistering occurred at the interface between the foamed sheet and the non-foamed film.

(比較例5)実施例1で得られたポリスチレン系樹脂発泡シートの密度0.45g/cm3 の面に、加熱ロールを60℃に加熱した後、熱風装置の250℃の風で加熱処理を施しした以外は、実施例1と同様にしてポリスチレン系樹脂積層シートを得た。得られた積層シートは発泡シートと非発泡フィルムの界面で火膨れが発生した。 (Comparative Example 5) A heating roll was heated to 60 ° C on the surface of the polystyrene-based resin foam sheet obtained in Example 1 having a density of 0.45 g / cm 3 , and then heat-treated with 250 ° C wind from a hot air device. A polystyrene-based resin laminate sheet was obtained in the same manner as in Example 1 except that it was applied. In the obtained laminated sheet, blistering occurred at the interface between the foamed sheet and the non-foamed film.

得られたポリスチレン系樹脂積層発泡シートから54cm角の単板を切り出した後、25℃の部屋に10日間単板養生後に、単発成形機を用いて、雰囲気温度(上/下)152/141℃設定で加熱秒数30秒時の火膨れ(成形加熱時にポリスチレン系樹脂発泡シートとフィルムとの間に剥離する現象)発生の有無を確認した。その際の評価基準は、以下のとおりである。
○:火膨れの発生が認められない。
×:火膨れの発生が認められる。
評価結果を表1に示した。
After cutting out a 54 cm square veneer from the obtained polystyrene-based resin laminated foam sheet, after curing the veneer for 10 days in a room at 25 ° C., using a single molding machine, the ambient temperature (up / down) 152/141 ° C. The presence or absence of occurrence of a blister (a phenomenon of peeling between the polystyrene resin foam sheet and the film during molding heating) at 30 seconds after heating was confirmed. The evaluation criteria at that time are as follows.
○: No occurrence of blistering is observed.
X: The occurrence of a blister is recognized.
The evaluation results are shown in Table 1.

Figure 2008114421
Figure 2008114421

本発明のポリスチレン系樹脂積層シートの製造方法において、火熱ロール及び熱風装置でポリスチレン系樹脂発泡シートの積層面を処理する工程を表す略図である。In the manufacturing method of the polystyrene-type resin lamination sheet of this invention, it is the schematic showing the process of processing the lamination surface of a polystyrene-type resin foam sheet with a hot roll and a hot air apparatus.

符号の説明Explanation of symbols

1:発泡シート
2:加熱ロール
3:熱風装置
4:ニップロール
5:冷却ロール
6:Tダイ
7:非発泡樹脂層
8:積層フィルム
9:エキスパンダーロール
10:積層発泡シート
1: Foam sheet 2: Heating roll 3: Hot air device 4: Nip roll 5: Cooling roll 6: T die 7: Non-foamed resin layer 8: Laminated film 9: Expander roll 10: Laminated foam sheet

Claims (3)

ポリスチレン系樹脂発泡シートに非発泡フィルムを積層してなるポリスチレン系樹脂積層シートの製造方法であって、ポリスチレン系樹脂発泡シートの積層面の表面温度が50℃以上70℃未満となるように予め加熱処理を行なった後、該処理を施した面に非発泡フィルムを積層することを特徴とするポリスチレン系樹脂積層シートの製造方法。   A method for producing a polystyrene-based resin laminated sheet obtained by laminating a non-foamed film on a polystyrene-based resin foamed sheet, which is preheated so that the surface temperature of the laminated surface of the polystyrene-based resin foamed sheet is 50 ° C. or higher and lower than 70 ° C. A process for producing a polystyrene-based resin laminate sheet, comprising: laminating a non-foamed film on the treated surface after the treatment. 前記非発泡フィルムが、ポリスチレン系樹脂の非発泡フィルムであることを特徴とする請求項1記載のポリスチレン系樹脂積層シートの製造方法。   The method according to claim 1, wherein the non-foamed film is a non-foamed film of polystyrene resin. 前記ポリスチレン系樹脂発泡シートの厚みが1mm以上3mm以下であり、前記非発泡フィルムの厚みが100μm以上200μm以下であることを特徴とする請求項1または2に記載のポリスチレン系樹脂積層シートの製造方法。   3. The method for producing a polystyrene-based resin laminated sheet according to claim 1, wherein the polystyrene-based resin foam sheet has a thickness of 1 mm to 3 mm, and the non-foamed film has a thickness of 100 μm to 200 μm. .
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013209445A (en) * 2012-03-30 2013-10-10 Sekisui Plastics Co Ltd Polystyrene-based resin foamed plate, method for producing the same, peripheral-side frame material for folding box, and the folding box
JP2015174390A (en) * 2014-03-17 2015-10-05 積水化成品工業株式会社 Polystyrene resin foaming sheet

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01171838A (en) * 1987-12-28 1989-07-06 Shonan Sekisui Kogyo Kk Manufacture of surface treatment product of foaming polystyrene sheet
JPH0361042A (en) * 1989-07-29 1991-03-15 Kanegafuchi Chem Ind Co Ltd Preparation of laminated sheet for molding container

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01171838A (en) * 1987-12-28 1989-07-06 Shonan Sekisui Kogyo Kk Manufacture of surface treatment product of foaming polystyrene sheet
JPH0361042A (en) * 1989-07-29 1991-03-15 Kanegafuchi Chem Ind Co Ltd Preparation of laminated sheet for molding container

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013209445A (en) * 2012-03-30 2013-10-10 Sekisui Plastics Co Ltd Polystyrene-based resin foamed plate, method for producing the same, peripheral-side frame material for folding box, and the folding box
JP2015174390A (en) * 2014-03-17 2015-10-05 積水化成品工業株式会社 Polystyrene resin foaming sheet

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