JPS6052929B2 - Method for manufacturing expanded polystyrene sheet - Google Patents
Method for manufacturing expanded polystyrene sheetInfo
- Publication number
- JPS6052929B2 JPS6052929B2 JP55021691A JP2169180A JPS6052929B2 JP S6052929 B2 JPS6052929 B2 JP S6052929B2 JP 55021691 A JP55021691 A JP 55021691A JP 2169180 A JP2169180 A JP 2169180A JP S6052929 B2 JPS6052929 B2 JP S6052929B2
- Authority
- JP
- Japan
- Prior art keywords
- polystyrene
- ring
- sheet
- cylindrical body
- heating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
- B29C44/50—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying
- B29C44/507—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying extruding the compound through an annular die
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2025/00—Use of polymers of vinyl-aromatic compounds or derivatives thereof as moulding material
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Molding Of Porous Articles (AREA)
Description
【発明の詳細な説明】
本発明は発泡ポリスチレンシートの製造方法に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing expanded polystyrene sheets.
発泡ポリスチレンシートは、一般に熱成形加工 され
て種々の食品包装容器、例えばトレイ、ラーメンカツプ
や弁当箱等に広く使用されている。Expanded polystyrene sheets are generally thermoformed and widely used in various food packaging containers, such as trays, ramen cups, and lunch boxes.
これらの容器の外観を改善したり、強度を向上させる目
的で発泡ポリスチレンシート表面に発泡の著しく抑制さ
れた樹脂層(以後未発泡層と呼ぶ。)を厚く付与すべく
、環状スリットより熔融押出された低沸点有機化合物を
含むポリスチレンを冷却してなる発泡ポリスチレンシー
トの製造方法が既に開発されている。 しかし、従来技
術によつて製造される厚い未発泡層を有する発泡ポリス
チレンシートは、強い配向を残している為に、加熱して
トレイ、ラーメンカツプや弁当箱を連続的に真空成形す
る際、シートの収縮しようとする力が強く、成形機のシ
ートクランプよりシートが外れ成形品が得られない欠点
や、成型機においてシートのくり返し強い収縮により、
クランプ部の摩耗および損傷を起す原因となり、その改
良が要請されている。In order to improve the appearance of these containers and improve their strength, polystyrene foam is melt-extruded through an annular slit in order to provide a thick resin layer with significantly suppressed foaming (hereinafter referred to as an unfoamed layer) on the surface of the sheet. A method for producing expanded polystyrene sheets by cooling polystyrene containing low-boiling organic compounds has already been developed. However, foamed polystyrene sheets with a thick unfoamed layer produced by conventional techniques retain strong orientation, so when heated and continuously vacuum-formed into trays, ramen cups, and lunch boxes, the sheets Due to the strong shrinkage force of the sheet, the sheet comes off from the molding machine's sheet clamp and a molded product cannot be obtained.Also, due to the repeated strong contraction of the sheet in the molding machine,
This causes wear and damage to the clamp part, and improvements are required.
本発明は厚い未発泡層を有し、環状スリットよ’り押
出され引取られる過程でシートの配向を緩和し、加熱成
形時の収縮する力の小さい改良された発泡ポリスチレン
シートを製造することを目的とするものである。The purpose of the present invention is to produce an improved foamed polystyrene sheet that has a thick unfoamed layer, relaxes the orientation of the sheet during the process of being extruded through an annular slit and is taken off, and has less shrinkage force during hot molding. That is.
本発明のこれらの課題を達成する為に、冷却リングの
使用とさらに加熱リングによる発泡ポリスチレンシート
表面の加熱が有効であることを見出し本発明を完全した
。In order to achieve these objects of the present invention, it was discovered that the use of a cooling ring and further heating of the surface of a foamed polystyrene sheet with a heating ring was effective, and the present invention was completed.
すなわち、本発明者はポリスチレンを低沸点有機化合物
と共に熔融混練せしめ、環状スリットより筒状体に押出
し、該筒状体の径を膨張させ、次いで切り開くことによ
り発泡ポリスチレンシートを得る方法に於いて、筒状体
の表面を環状スリットの直後方に(すなわち樹脂の進行
方向に向つて前側)に設置した−10〜90′Cに保持
した冷却リングに接触させ、ポリスチレンの加熱変形温
度±10℃の範囲まで冷却せしめ、次いで冷却リングの
直後方に設置した加熱変形温度±10℃以上に保たれた
加熱リングに接触させることを特徴とするものである。That is, the present inventor has developed a method for obtaining a foamed polystyrene sheet by melt-kneading polystyrene with a low-boiling organic compound, extruding it into a cylindrical body through an annular slit, expanding the diameter of the cylindrical body, and then cutting it open. The surface of the cylindrical body was brought into contact with a cooling ring maintained at -10 to 90'C, which was installed immediately behind the annular slit (that is, on the front side in the direction of resin progression), and the heating deformation temperature of polystyrene was adjusted to ±10°C. It is characterized in that it is cooled to a temperature within a range of 100° C. and then brought into contact with a heating ring that is placed immediately behind the cooling ring and maintained at a heating deformation temperature of ±10° C. or higher.
以下、本発明の内容を更に詳細に説明する。本発明で使
用されるポリスチレンはスチレンを主成分とする熱可塑
性合成樹脂であり、汎用ポリスチレンの他の耐衝撃性ポ
リスチレン、ブロムスチレンやα−メチルスチレンとの
共重合ポリスチレン、無水マレイン酸との共重合ポリス
チレン等が含まれる。また、本発明に使用するポリスチ
レンに気泡の大きさを調節する為にタルク、シリカゲル
、炭酸カルシウム等の無機物を少量含むことは何ら差支
えない。本発明に使用される低沸点有機化合物とは、ポ
リスチレンの発泡剤として一般に用いられているもので
あつて、例えば、プロパン、ブタン、ペンタン、ヘキサ
ン等の炭化水素化合物や、フレオンー11、フレオンー
12、フレオンー113sフレオンー11屯クロロホル
ム、メチルクロライド、メチレンクロライド等のハロゲ
ン化炭化水素化合物、石油エーテル等が代表的であり、
低沸点有機化合物が通常ポリスチレン100yに対して
0.02〜0.07モル加える。Hereinafter, the content of the present invention will be explained in more detail. The polystyrene used in the present invention is a thermoplastic synthetic resin whose main component is styrene, and it can be used in combination with general-purpose polystyrene, other impact-resistant polystyrene, copolymerized polystyrene with bromustyrene and α-methylstyrene, and copolymerized polystyrene with maleic anhydride. Includes polymerized polystyrene, etc. Further, the polystyrene used in the present invention may contain a small amount of an inorganic substance such as talc, silica gel, calcium carbonate, etc. in order to adjust the size of bubbles. The low-boiling organic compounds used in the present invention are those commonly used as blowing agents for polystyrene, such as hydrocarbon compounds such as propane, butane, pentane, hexane, Freon-11, Freon-12, Freon-113s Freon-11ton Chloroform, methyl chloride, methylene chloride, and other halogenated hydrocarbon compounds, petroleum ether, etc. are typical examples.
The low boiling point organic compound is usually added in an amount of 0.02 to 0.07 mol per 100y of polystyrene.
また、炭酸アンモニウム、重炭酸ナトリウム等の無機系
化学発泡剤や、アゾジカルボンアミド、アゾビスホルム
アミド、N−N″−ジニトロソペンタメチレンテトラミ
ン、P−トルエンスルホニルヒドラジド等の有機系化学
発泡剤を少量併用し・ても、何ら差支えない。In addition, small amounts of inorganic chemical blowing agents such as ammonium carbonate and sodium bicarbonate, and organic chemical blowing agents such as azodicarbonamide, azobisformamide, N-N''-dinitrosopentamethylenetetramine, and P-toluenesulfonyl hydrazide are used. There is no problem in using them together.
本発明でいう冷却リングとは、環状スリットより押出さ
れた樹脂の筒状体の外側又は内側に設置、該筒状体に表
面を冷却するものであつて、筒状体との接触面は該筒状
体の外径又は内径の膨張に合致する形であつて該筒状体
の進行方向に対し、ラツパ状に広がつているものである
。The cooling ring in the present invention is installed on the outside or inside of a resin cylinder extruded through an annular slit to cool the surface of the cylinder, and the contact surface with the cylinder is It has a shape that matches the expansion of the outer diameter or inner diameter of the cylindrical body, and expands in a tapered manner in the direction of movement of the cylindrical body.
該冷却リングの例としては、内部に冷却媒体を通す循環
路を有する接触面の平滑な冷却リングや筒状体との接触
面か冷却媒体のしみ出る多孔質の構造体を有する冷却リ
ング等がある。Examples of the cooling ring include a cooling ring with a smooth contact surface having a circulation path for passing a cooling medium therein, and a cooling ring having a porous structure from which the cooling medium seeps from the contact surface with the cylindrical body. be.
冷却リングの温度は付与する未発泡層の厚さを決める因
子の一つであつて、筒状体との接触面積)や引取速度に
より規定される。The temperature of the cooling ring is one of the factors that determines the thickness of the unfoamed layer to be applied, and is determined by the contact area with the cylindrical body and the take-up speed.
20μ以上の充分な厚みの未発泡層を付与するには、筒
状体の表面を加熱変形温度±10℃まで冷却する必要が
あり、その為には、通常、冷却リングの温度は−10〜
90℃に保たれる。In order to provide an unfoamed layer with a sufficient thickness of 20μ or more, it is necessary to cool the surface of the cylindrical body to the heating deformation temperature ±10℃, and for this purpose, the temperature of the cooling ring is usually -10~10℃.
It is kept at 90℃.
−10℃未満では、冷却リングの筒状・体との接触面積
をどんなに小さくしても、均一に未発泡層を付与した発
泡ポリスチレンシートを得ることが出来ない。また逆に
、90℃以上では接触面積をいかに大きくしても未発泡
層を20μ以上付与することができない。ここで加熱変
形温度は・縦、横、厚さが127×(12.7±0.2
)×(6.4±0.2)TgLである試験片を使用し、
JISK−6871−1961の試験法に準じて測定さ
れるものである。また、上記例示の場合の多孔質の構造
体には、ガラスフィルター、焼結金属、不織布等があり
、該冷却リングの目の粗さは、特に制約はないが、全周
より冷却媒体が均一にしみ出て、微細に冷却媒体を分散
する為に、通常、100メッシュ以上のものが使用され
る。冷却媒体としては、通常水が使用され、アルコール
等の表面張力や気化熱を調節する物質、さらに、帯電防
止剤や着色剤を添加したものを使用してもよい。本発明
でいう加熱リングとは筒状体の径を膨張する過程で、冷
却リングに接触した後、引き続き、接触するように設置
したものであつて、加熱リング内部に加熱媒体の循環路
を有し、加熱媒体により加熱するものや、電熱ヒーター
で加熱するもの等がある。If the temperature is less than -10°C, no matter how small the contact area with the cylindrical body of the cooling ring, it is impossible to obtain a foamed polystyrene sheet uniformly provided with an unfoamed layer. On the other hand, at temperatures above 90° C., no matter how large the contact area is, it is not possible to form an unfoamed layer of 20 μm or more. Here, the heating deformation temperature is 127×(12.7±0.2
)×(6.4±0.2)TgL using a test piece,
It is measured according to the test method of JISK-6871-1961. In addition, the porous structure in the case of the above example includes a glass filter, sintered metal, nonwoven fabric, etc., and there is no particular restriction on the roughness of the cooling ring, but the cooling medium is uniform from the entire circumference. In order to seep out and finely disperse the cooling medium, a material with a mesh size of 100 mesh or more is usually used. As the cooling medium, water is usually used, and a substance such as alcohol that adjusts surface tension and heat of vaporization, as well as an antistatic agent and a coloring agent, may be used. The heating ring referred to in the present invention is a cylindrical body that is placed in contact with the cooling ring during the process of expanding its diameter and continues to be in contact with the cooling ring, and has a heating medium circulation path inside the heating ring. However, there are those that are heated with a heating medium and those that are heated with an electric heater.
加熱リングの温度−は発泡ポリスチレンシートの配向を
緩和する程度により規定され、さらに筒状体との接触面
積や引取速度によつて決定されるが、ポリスチレンの加
熱変形温度+10℃以上なければならない。The temperature of the heating ring is determined by the extent to which the orientation of the foamed polystyrene sheet is relaxed, and is further determined by the contact area with the cylindrical body and the take-up speed, but must be at least 10° C. above the heating deformation temperature of the polystyrene.
加熱変形温度+10℃未満では、発泡ポリスチレンシー
トの配向が緩和されない。また加熱リングの上限温度は
、引き取られている発泡ポリスチレンシートの表面が融
着しない温度である。尚、本発明の冷却リングに引き続
き、加熱リングを設置して発泡ポリスチレンシートを製
造するにあたり、シートの厚み調整あるいは筒状体を膨
張させる目的で、エアーリングを併用することは、本発
明の範囲に包含されるものである。If the heating deformation temperature is lower than +10° C., the orientation of the expanded polystyrene sheet will not be relaxed. Moreover, the upper limit temperature of the heating ring is a temperature at which the surface of the expanded polystyrene sheet being pulled does not fuse. It should be noted that, when manufacturing a foamed polystyrene sheet by installing a heating ring following the cooling ring of the present invention, it is within the scope of the present invention to use an air ring in combination for the purpose of adjusting the thickness of the sheet or expanding the cylindrical body. It is included in.
次に、本発明を図面によつて説明する。第1図は、本発
明の実施の態様一つであつて、冷却リングと加熱リング
を筒状体の外側に設置したものである。Next, the present invention will be explained with reference to the drawings. FIG. 1 shows one embodiment of the present invention, in which a cooling ring and a heating ring are installed outside a cylindrical body.
ポリスチレンと低沸点有機化合物は、図外の押出機によ
つて熔融混練され、ダイ1の環状スリット2から押出さ
れる。ダイ1は押出機の先端に取付けられ、100〜1
70℃に加熱されている。押出された筒状体(樹脂)3
は、冷却リング4に接触を開始し、筒状体3の表面は、
ポリスチレンの加熱変形温度±10℃の範囲の温度まで
冷却され、表面には、20μ以上の充分なる未発泡層が
付与される。冷却リング4は、環状スリット2の直後方
に、ダイ1と接触しないだけの空隙を有して設置され、
その内部には冷却媒体を通す循環路5を有し図外の冷却
媒体循環装置によつて循環されている冷却媒体によつて
−10〜90℃の範囲の適当な温度に保たれている。冷
却リング4に接触した後、筒状体7は、加熱リング6に
接触する。加熱リング6は、内部に加熱媒体の通る循環
路7を有し、図外の加熱媒体循環装置によつて循環され
ている加熱媒体によつて、加熱変形温度+10℃以上の
適当な温度に保たれている。次いで、筒状体3は、10
〜30゜Cの冷却水の通つた冷却ドラム8により冷却固
化され、次いで、図外のスリツターにより切り開かれ、
捲取ロールに捲取られる。一方、ダイ1と冷却ドラム8
と筒状体3によつてつくられる空洞9には、空気吹込管
10より、空気を吐出させて、空洞9内の空気圧を高め
る。その空気圧によつて筒状体3は、図示した通り、冷
却リング4および加熱リング6の内壁面に押付けられつ
つ、内径を膨張させられ、冷却ドラム8に達し、完全に
冷却固化される。かくして、筒状体3は外側面に未発泡
層を付与され、かつ、加熱収縮する力の緩和された発泡
ポリスチレンシートとなる。なお、第1図では加熱リン
グを冷却リングと離して設置してあるが、未発泡層の付
与された筒状体を加熱リングに長い時間接触させる為に
、断熱材を介して加熱リングを冷却リングに連接して設
置しても何ら差支えない。次に、第2図は、別の実施の
態様であつて、冷却リングと加熱リングを筒状体の内側
に設置し、またエアーリング11の一例を併用したもの
である。Polystyrene and a low-boiling organic compound are melt-kneaded by an extruder (not shown) and extruded through an annular slit 2 of a die 1. Die 1 is attached to the tip of the extruder and has a diameter of 100 to 1
It is heated to 70°C. Extruded cylindrical body (resin) 3
starts contacting the cooling ring 4, and the surface of the cylindrical body 3 is
It is cooled to a temperature in the range of ±10° C., the heat deformation temperature of polystyrene, and a sufficient unfoamed layer with a thickness of 20 μm or more is provided on the surface. The cooling ring 4 is installed immediately behind the annular slit 2 with a gap large enough to prevent it from coming into contact with the die 1.
It has a circulation path 5 for passing a cooling medium therein, and is maintained at an appropriate temperature in the range of -10 to 90 DEG C. by the cooling medium being circulated by a cooling medium circulation device (not shown). After contacting the cooling ring 4, the tubular body 7 contacts the heating ring 6. The heating ring 6 has a circulation path 7 through which a heating medium passes inside, and is maintained at an appropriate temperature above the heating deformation temperature +10°C by the heating medium being circulated by a heating medium circulation device (not shown). It's dripping. Next, the cylindrical body 3 has 10
It is cooled and solidified by a cooling drum 8 through which cooling water of ~30°C is passed, and then cut open by a slitter (not shown).
It is rolled up on a winding roll. On the other hand, die 1 and cooling drum 8
Air is discharged from an air blowing pipe 10 into the cavity 9 formed by the cylindrical body 3 to increase the air pressure inside the cavity 9. The air pressure causes the cylindrical body 3 to expand its inner diameter while being pressed against the inner wall surfaces of the cooling ring 4 and the heating ring 6, and reaches the cooling drum 8, where it is completely cooled and solidified. In this way, the cylindrical body 3 becomes a foamed polystyrene sheet having an unfoamed layer on the outer surface and having a reduced heat-shrinking force. In Figure 1, the heating ring is installed separately from the cooling ring, but in order to keep the cylindrical body with the unfoamed layer in contact with the heating ring for a long time, the heating ring is cooled through a heat insulating material. There is no problem in installing it connected to the ring. Next, FIG. 2 shows another embodiment in which a cooling ring and a heating ring are installed inside a cylindrical body, and an example of an air ring 11 is also used.
筒状体3は、環状スリット2から押出されて、発泡開始
すると同時に、冷却リング4に接触し、次いで、加熱リ
ング6に接触し、径は膨張させられ、冷却ドラム8によ
つて冷却固化され、その後、切り開かれて、発泡ポリス
チレンシートとして得られる。The cylindrical body 3 is extruded from the annular slit 2 and starts foaming, and at the same time contacts the cooling ring 4 and then the heating ring 6, expands its diameter, and is cooled and solidified by the cooling drum 8. , and then cut open to obtain expanded polystyrene sheets.
本発明は得られた発泡ポリスチレンシートは、未発泡層
を30μ以上有していると同時に、押出し直後に冷却す
ることによりついた配向が加熱リングにより緩和し、加
熱収縮力が加熱リングを使用しない方法で得たシートに
比べ115〜112と減少したものであり、二次加工す
る際発生していた。The foamed polystyrene sheet obtained in the present invention has an unfoamed layer of 30μ or more, and at the same time, the orientation created by cooling immediately after extrusion is relaxed by the heating ring, and the heating shrinkage force is reduced without using the heating ring. This was a decrease of 115 to 112 compared to the sheet obtained by the method, and was generated during secondary processing.
加熱時、シートクランプより外れる問題点が解消され、
また収縮力の低下により、クランプ部の摩耗および損傷
が著しく減少した。更に本発明では環状スリットより押
出された筒状体が、冷却リングに接触した後膨張する過
程において、未発泡層が膨張しきれず割れを生する従来
技術の欠点も除去でき、未発泡層がさらに厚く付与でき
る。また、本発明では、加熱リングを使用している為に
、発泡ポリスチレンシートの表面の平滑性が改善され、
光択が増し、印刷性も向上する効果も得られ”た。この
様に、本発明に厚い未発泡層を有する発泡ポリスチレン
シートを製造する上で価値の高いものである。The problem of the seat clamp coming off when heated has been resolved.
Also, due to the reduction in shrinkage force, wear and damage to the clamp part was significantly reduced. Furthermore, the present invention eliminates the drawback of the prior art in which the unfoamed layer does not fully expand and cracks occur during the expansion process of the cylindrical body extruded from the annular slit after contacting the cooling ring, and the unfoamed layer further expands. Can be applied thickly. In addition, since the present invention uses a heating ring, the surface smoothness of the expanded polystyrene sheet is improved.
The effect of increasing photo selectivity and improving printability was also obtained. As described above, the present invention is of high value in producing a foamed polystyrene sheet having a thick unfoamed layer.
なお、加熱収縮とは、規定の大きさ、例えば、500×
100mにした発泡ポリスチレンシ+を1000C以上
に加熱された乾燥機中に放置した時、シート内に存在す
る残留応力が、シート自身を締めようとする力である。Note that heat shrinkage refers to a specified size, for example, 500×
When expanded polystyrene + made to a length of 100 m is left in a dryer heated to 1000 C or more, the residual stress existing within the sheet is a force that tries to tighten the sheet itself.
本発明の説明で使用している加熱収縮力の値は、500
×100Tfnの試験片を150℃のノ乾燥機中に放置
した時の最大値てある。次に実施例により、本発明の具
体的に説明する。The value of the heat shrinkage force used in the explanation of the present invention is 500
The maximum value is shown when a test piece of ×100Tfn is left in a dryer at 150°C. Next, the present invention will be specifically explained with reference to Examples.
実施例1
第1図に示した通りの設備を用い、ポリスチレン1(4
)部とタルク0.5部とを混合し、90Tnφの押出機
にて熔融混練させ、次いで該押出機の途中に設けた注入
口よりブタンをポリスチレン100yに対して0.05
モルの割合で圧入混合させ、135℃に設定した押出口
に設けた60順φの環状スリットより、大気中に筒状体
として押出した。Example 1 Polystyrene 1 (4
) part and 0.5 part of talc were mixed and melted and kneaded in a 90Tnφ extruder, and then 0.05 parts of butane was added to 100y of polystyrene through an injection port provided in the middle of the extruder.
The mixture was press-mixed in a molar ratio and extruded as a cylindrical body into the atmosphere through an annular slit with a diameter of 60 in the order provided in an extrusion port set at 135°C.
環状スリットのすぐ後に30℃に保つた接触面積150
cItの冷却リングを筒状体の外表面に接触するように
設置し、次いで、130℃に保つた接触面積100cI
tの加熱リングを筒状体の外表面に接触するように設置
し、筒状体の外表面に未発泡層を形成させた後筒状体の
配向を緩和させながら膨張させ、その後直径207W$
Lの200Cに保つた冷却ドラムに5n1/Min.の
速度で引取り、冷却固化させた。この様にして得られた
坪量200y/7nのシートは、巾が650Tf1m1
厚さが1.2TIr!nで片面に未発泡層が70μ形成
していた。このシートは、加熱収縮力が210Vとなり
、連続真空成形する際、成形機のシートクランプから外
れる問題を生じないし、シート表面は未発泡層,の割れ
もなく、光沢があり、外観上優れたものであつた。Contact area 150 kept at 30°C immediately after the annular slit
A cooling ring of cIt was placed in contact with the outer surface of the cylindrical body, and then a contact area of 100 cI was maintained at 130°C.
A heating ring t was placed in contact with the outer surface of the cylindrical body, and after forming an unfoamed layer on the outer surface of the cylindrical body, the cylindrical body was expanded while relaxing its orientation, and then the diameter was 207 W$.
5n1/Min.L cooling drum maintained at 200C. It was taken at a speed of The sheet with a basis weight of 200y/7n obtained in this way has a width of 650Tf1m1
Thickness is 1.2TIr! An unfoamed layer of 70 μm was formed on one side. This sheet has a heating shrinkage force of 210V, so there is no problem of it coming off from the sheet clamp of the molding machine during continuous vacuum forming, and the sheet surface has a glossy appearance with no cracks in the unfoamed layer. It was hot.
比較例1
実施例1の設備において、加熱リングを取り除き、冷却
リングの温度を30゜Cとし、発泡ポリスチレンシート
を製造した。Comparative Example 1 In the equipment of Example 1, the heating ring was removed and the temperature of the cooling ring was set to 30°C to produce a foamed polystyrene sheet.
得られたシートは110℃の温度に保つた加熱リングを
取付けて製造したシートのシート厚、未発泡層厚とほぼ
同値てあるが、加熱収縮力は380yで、加熱リングに
接触させて得たシートに比べ約80%高く、トレー成形
機にて加熱するとシートクランプより外れてしまつた。The thickness of the obtained sheet was almost the same as that of the sheet produced by attaching a heating ring kept at a temperature of 110°C, and the thickness of the unfoamed layer, but the heating shrinkage force was 380y, which was obtained by contacting with the heating ring. It was about 80% more expensive than a sheet, and when heated in a tray molding machine, it came off from the sheet clamp.
第1図および第2図は、本発明の実施の態様の例を説明
するための断面略図である。
1・・・・・・ダイ、2・・・・・・環状スリット、3
・・・・・・筒状体、4・・・・・・冷却リング、5・
・・・・・冷却媒体循環路、6・・・・・・加熱リング
、7・・・・・・加熱媒体循環路、8・・・・・・冷却
ドラム、9・・・・・・空洞、10・・・・・・空気吹
込管、11・・・・・・エアーリング。1 and 2 are schematic cross-sectional views for explaining examples of embodiments of the present invention. 1...Die, 2...Annular slit, 3
......Cylindrical body, 4...Cooling ring, 5.
... Cooling medium circulation path, 6 ... Heating ring, 7 ... Heating medium circulation path, 8 ... Cooling drum, 9 ... Cavity , 10... Air blowing pipe, 11... Air ring.
Claims (1)
しめ、環状スリットより筒状体に押出し、該筒状体の径
を膨張させ、次いで切り開くことにより発泡ポリスチレ
ンシートを得る方法に於いて、筒状体の表面を環状スリ
ットの直後方に設置した−10〜90℃に保持した冷却
リングに接触させ、ポリスチレンの加熱変形温度±10
℃の範囲まで冷却せしめ、次いで冷却リングの直後方に
設置した加熱変形温度+10℃以上に保たれた加熱リン
グに接触させることを特徴とする発泡ポリスチレンシー
トの製造方法。 2 ポリスチレンが、汎用ポリスチレン、耐衝撃性ポリ
スチレン、ブロムスチレンやα−メチルスチレンとの共
重合ポリスチレンまたは、無水マレイン酸との共重合ポ
リスチレンである特許請求の範囲第1項記載の製造方法
。 3 加熱リングが断熱材を介して冷却リングに隣接して
設置されている特許請求の範囲第1項記載の製造方法。[Claims] 1. A method for obtaining a foamed polystyrene sheet by melt-kneading polystyrene with a low-boiling organic compound, extruding it into a cylindrical body through an annular slit, expanding the diameter of the cylindrical body, and then cutting it open. Then, the surface of the cylindrical body was brought into contact with a cooling ring maintained at -10 to 90°C installed immediately behind the annular slit, and the heating deformation temperature of polystyrene was ±10°C.
A method for manufacturing a foamed polystyrene sheet, which comprises cooling the sheet to a temperature within the range of 10°C, and then bringing it into contact with a heating ring placed immediately behind the cooling ring and maintained at a heating deformation temperature +10°C or higher. 2. The manufacturing method according to claim 1, wherein the polystyrene is general-purpose polystyrene, impact-resistant polystyrene, copolymerized polystyrene with bromustyrene or α-methylstyrene, or copolymerized polystyrene with maleic anhydride. 3. The manufacturing method according to claim 1, wherein the heating ring is installed adjacent to the cooling ring via a heat insulating material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55021691A JPS6052929B2 (en) | 1980-02-25 | 1980-02-25 | Method for manufacturing expanded polystyrene sheet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55021691A JPS6052929B2 (en) | 1980-02-25 | 1980-02-25 | Method for manufacturing expanded polystyrene sheet |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56118829A JPS56118829A (en) | 1981-09-18 |
| JPS6052929B2 true JPS6052929B2 (en) | 1985-11-22 |
Family
ID=12062085
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55021691A Expired JPS6052929B2 (en) | 1980-02-25 | 1980-02-25 | Method for manufacturing expanded polystyrene sheet |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6052929B2 (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5867422A (en) * | 1981-10-19 | 1983-04-22 | Sekisui Plastics Co Ltd | Extrusion expanding polystyrene resin sheet |
| US4465649A (en) * | 1982-12-20 | 1984-08-14 | Mobil Oil Corporation | Method and system for extruding tubular foamed polymer sheet |
| JPS62211133A (en) * | 1986-03-12 | 1987-09-17 | Kanegafuchi Chem Ind Co Ltd | Styrene series resin extruded foamed body, excellent in dimensional stability, and manufacture thereof |
| JPH0628889B2 (en) * | 1986-11-11 | 1994-04-20 | 積水化成品工業株式会社 | Method for producing styrene resin foam sheet |
| JP2500586Y2 (en) * | 1992-02-20 | 1996-06-05 | 積水化成品工業株式会社 | Polystyrene resin foam sheet |
| JP5449058B2 (en) * | 2009-09-18 | 2014-03-19 | 積水化成品工業株式会社 | Method for producing styrene resin foam sheet |
| JP5618403B2 (en) * | 2010-01-08 | 2014-11-05 | 積水化成品工業株式会社 | Method for producing polystyrene resin foam sheet and method for producing foamed molded product |
| JP5793386B2 (en) * | 2011-02-28 | 2015-10-14 | 積水化成品工業株式会社 | Polystyrene resin foam sheet and molded product |
| JPWO2024075632A1 (en) * | 2022-10-06 | 2024-04-11 |
-
1980
- 1980-02-25 JP JP55021691A patent/JPS6052929B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56118829A (en) | 1981-09-18 |
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