JPS59179633A - Polystyrene sheet foam for forming deep-drawn container - Google Patents
Polystyrene sheet foam for forming deep-drawn containerInfo
- Publication number
- JPS59179633A JPS59179633A JP58057518A JP5751883A JPS59179633A JP S59179633 A JPS59179633 A JP S59179633A JP 58057518 A JP58057518 A JP 58057518A JP 5751883 A JP5751883 A JP 5751883A JP S59179633 A JPS59179633 A JP S59179633A
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- polystyrene
- foam
- resin
- sheet foam
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Laminated Bodies (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、深絞シ容器成形用ポリスチレン系発泡シー
トに関する。 さらに詳しくは、コツプ状成形体等の深
絞シ容器のシート成形用の原反であって優れた成形性を
有し、ことに大量生産用の原反として有利な深絞シ容器
成形用ポリスチレン系発泡シートに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a polystyrene foam sheet for forming deep-drawn containers. More specifically, polystyrene for forming deep-drawn containers, which is a raw material for sheet forming of deep-drawn containers such as pot-shaped molded bodies, has excellent moldability, and is especially advantageous as a raw material for mass production. The present invention relates to a foam sheet.
従来から、ポリスチレン発泡成形品を製造する方法の一
つとして押出機を用いた方法が知られている。 この方
法は、ポリスチレン樹脂組成物を発泡剤と共に押出様か
ら押出発泡ζせてシート状(原反)とし、これを該シー
トの軟化点以上に加熱すると共に成形型に供給するシー
ト成形のごとき二次成形に付して行なう方法である。
この方法によって種々の成型品が製造されている。Conventionally, a method using an extruder has been known as one of the methods for manufacturing polystyrene foam molded products. This method involves extrusion foaming of a polystyrene resin composition together with a foaming agent to form a sheet (original fabric), which is heated above the softening point of the sheet and then fed into a mold. This method is performed after subsequent molding.
Various molded products are manufactured by this method.
しかしかような成形方法には、シートの二次成形性に伴
なう種々の問題点があった。 すなわち、二次成形時の
加熱によるシートの二次発泡によって、成形金型に対す
る成形品の寸法精度や寸法安定性(以下型の出n )が
不充分となり嵌め込み蓋等の成形が困難であること、加
熱時のシートの伸びに限界がありコツプ等の深絞り容器
の成形の自由度が極端に制限されることなどの問題点が
あった。 とくに従来のポリスチレン系発泡シートを用
い絞り比1以上のコツプ状容器を連続的に製造する場合
には、シートの伸びの限界により第8図に示すように少
なくとも各成形型間には充分な余裕を設定する必要があ
り、原反からの成形品生産効率が悪いという不都合があ
った。 ことにコツプ状容器は最近、カップめん等の食
品容器として大量に用いられるため、原反から効率良く
成形品を得ること、言い換れば同一面積の原反から所望
の成形品をより多く得ることが切望されていた。However, such a forming method has various problems associated with the secondary formability of the sheet. In other words, due to secondary foaming of the sheet due to heating during secondary molding, the dimensional accuracy and dimensional stability of the molded product relative to the molding die (hereinafter referred to as "mold ejection n") is insufficient, making it difficult to mold a fitted lid, etc. However, there was a problem in that there was a limit to the elongation of the sheet during heating, and the degree of freedom in forming deep-drawn containers such as cots was extremely limited. In particular, when conventional polystyrene foam sheets are used to continuously manufacture pot-shaped containers with a drawing ratio of 1 or more, due to the limit of sheet elongation, at least sufficient space must be provided between each mold as shown in Figure 8. It was necessary to set the following parameters, which had the disadvantage that the production efficiency of molded products from the original fabric was poor. In particular, cup-shaped containers have recently been used in large quantities as food containers for cup noodles and the like, so it is important to efficiently obtain molded products from raw fabric, or in other words, to obtain more desired molded products from the same area of raw fabric. was desperately needed.
この発明は、かような従来の問題点に鑑みなされたもの
であり、所望の深絞り容器が従来に比して効率良く得ら
れる成形用原反を提供することを一つの目的とするもの
である。This invention has been made in view of the above-mentioned conventional problems, and one of its objects is to provide a raw fabric for forming that allows a desired deep-drawn container to be obtained more efficiently than in the past. be.
木発明者らは先に発泡剤の残ガス量を0.3モル/kg
以下に制御した特定のポリスチレン系発泡シートが、ト
レイ等の成形品用原反として極めて適している事実を見
出した。 この発明は、残ガス量0.8モル/kg以下
のポリスチレン系発泡シートについて更に別の観点から
検討を行なう結果見い出されたものである。The wood inventors first determined that the amount of residual gas in the blowing agent was 0.3 mol/kg.
We have discovered that a specific polystyrene foam sheet controlled as follows is extremely suitable as a raw material for molded products such as trays. This invention was discovered as a result of studies conducted from a different perspective on polystyrene foam sheets having a residual gas amount of 0.8 mol/kg or less.
かくしてこの発明によればポリスチレン系樹脂を基材樹
脂とするシート状発泡体の少なくとも一面に非発泡樹脂
フィルムを81を層した厚みl〜Bmyxの機台シート
からなり、上記シート状発泡体は基材樹脂に対して1〜
30重量%相当のゴム成分及び1〜20重量%相当の充
填材を含有しかつ発泡剤の残ガス量が01モル/kg以
下に制御されたシート状発泡体からなり、上記非発泡樹
脂フィルムは厚へ5〜600μmの熱可塑性樹脂フィル
ムからなることを特徴とする深絞り容器成形用ポリスチ
レン系発泡シートが提供される。Thus, according to the present invention, a base sheet having a thickness of 1 to Bmyx is formed by layering a non-foamed resin film 81 on at least one surface of a sheet-like foam whose base resin is polystyrene resin, and the sheet-like foam has a base material of 1~ for material resin
The non-foamed resin film is made of a sheet-like foam containing a rubber component equivalent to 30% by weight and a filler equivalent to 1 to 20% by weight, and in which the residual gas amount of the blowing agent is controlled to 0.1 mol/kg or less. A polystyrene foam sheet for forming deep-drawn containers is provided, which is characterized by being made of a thermoplastic resin film having a thickness of 5 to 600 μm.
以下、添付図面の具体例と共にこの発明の発泡シートに
ついて詳説する。Hereinafter, the foamed sheet of the present invention will be explained in detail with reference to specific examples shown in the accompanying drawings.
第1図は、この発明の深絞シ容器成形用ポリスチレン系
発泡シート(1)を示す断面図である。 図において発
泡シート(1)は、ポリスチレン系樹脂を基材樹脂とす
るシート状発泡体(2)の−面に非発泡樹脂フィルム(
3)を融着積層した厚み1〜3間の複合シートからなる
。 そしてシート状発泡体(2)は基材樹脂に対して1
〜30重量%相当のゴム成分と同じく1〜20重量%相
当の充填材を含有してなりかつ揮発性発泡剤の残ガス量
が0.3モル/kg以下に制御されてなる。 一方、非
発泡樹脂フィルム(3)ハ厚み5〜600μmの熱可塑
性樹脂フィルムからなる。FIG. 1 is a sectional view showing a polystyrene foam sheet (1) for deep-drawn container molding of the present invention. In the figure, a foamed sheet (1) is a non-foamed resin film (
It consists of a composite sheet with a thickness of 1 to 3, which is obtained by laminating 3) by fusion bonding. And the sheet-like foam (2) has a ratio of 1 to the base resin.
It contains a rubber component equivalent to ~30% by weight and a filler equivalent to 1~20% by weight, and the residual gas amount of the volatile blowing agent is controlled to 0.3 mol/kg or less. On the other hand, the non-foamed resin film (3) is made of a thermoplastic resin film having a thickness of 5 to 600 μm.
かようなこの発明の発泡シートは深絞りの成形用として
極めて良好な成形性を示し、ことに第2図に示すごとく
絞り比(b/a )が1.0以上の極めて深絞シのコツ
プ状成形品(4)を、所望強度を失なうことなく簡便に
得ることができる。 さらに従来に比して同じ大きさの
原反から多数の成形品を効率良く生産することができる
。 例えば、従来のポリスチレンシートからなる600
avX600朋の原反(非発泡樹脂フィルムラミネート
品を含む)から、口径92騎、深さ1051の第2図に
示すごときコツプ状成形品(4)を作jlj11する際
、従来の成形用シー)(l’)ではせいぜい第3図に示
すととく4×4の16個取りが限度であったが、この発
明の発泡シートによれば第4図に示すとと〈5×5の2
5個取りが可能となり、それ以上の密な型取りも可能で
ある。The foamed sheet of this invention exhibits extremely good formability for deep drawing, and is especially suitable for deep drawing with a draw ratio (b/a) of 1.0 or more, as shown in FIG. A shaped article (4) can be easily obtained without losing the desired strength. Furthermore, a large number of molded products can be produced more efficiently from the same size of original fabric than in the past. For example, 600 sheets made of conventional polystyrene sheet
When making a pot-shaped molded product (4) as shown in Fig. 2 with a diameter of 92mm and a depth of 1051mm from the original fabric of avX600 (including non-foamed resin film laminate products), use a conventional molding sheet). (l'), as shown in FIG.
It is possible to make 5 pieces, and it is also possible to make more dense molds.
この発明のシート状発泡体の基材樹脂であるポリスチレ
ン系樹脂とはスチレン、メチルスチレン、ジメチルスチ
レン等のスチレン系ビニルモノマーを主構成単位とする
重合体を示すものであり、他のビニルモノマー、例えば
アクリル酸、メタクリル酸もしくはこれらのエステル、
アクリロニトリル、アクリルアミド、メタクリルニトリ
ル、無水マレイン酸等との共重合体であってもよい。The polystyrene resin that is the base resin of the sheet-like foam of this invention refers to a polymer whose main constituent unit is a styrene vinyl monomer such as styrene, methylstyrene, or dimethylstyrene, and other vinyl monomers, For example, acrylic acid, methacrylic acid or esters thereof,
It may also be a copolymer with acrylonitrile, acrylamide, methacrylnitrile, maleic anhydride, or the like.
このポリスチレン系樹脂とゴム成分と充填材とを含有す
る樹脂組成物を押出発泡成形に付すことにより、この発
明におけるシート状発泡体が得られる。The sheet-like foam of the present invention is obtained by subjecting the resin composition containing this polystyrene resin, rubber component, and filler to extrusion foam molding.
上記ゴム成分は、上記ポリスチレン系樹脂に対しブレン
ド成分又は共重合成分として1〜30重量%含有される
。 ゴム成分としては種々のものが用いられるが、ブレ
ンド成分として用いる場合ニハフタジエンゴム、エチレ
ン−プロピレンゴム、スチレン−ブタジェンゴム、ポリ
エチレン等ヲ前記ポリスチレン系樹脂に添加して用いる
のが適当であり、共重合成分として用いる場合には、ブ
タジェン、イソプレン、クロロブレン等のモノマー又は
オリゴマーを所定のモル比で共重合してなるポリスチレ
ン系樹脂を用いるのが適当である(なお、この場合、ポ
リスチレン系樹脂として共重合体を用いた場合にはゴム
成分を含めてターポリマーの状態となることが理解され
るであろう。)。The rubber component is contained in an amount of 1 to 30% by weight based on the polystyrene resin as a blend component or copolymer component. Various rubber components can be used, but when used as a blend component, it is appropriate to add nihaftadiene rubber, ethylene-propylene rubber, styrene-butadiene rubber, polyethylene, etc. to the polystyrene resin. When used as a polymerization component, it is appropriate to use a polystyrene resin made by copolymerizing monomers or oligomers such as butadiene, isoprene, chlorobrene, etc. in a predetermined molar ratio (in this case, copolymerization as a polystyrene resin) is appropriate. It will be understood that when a polymer is used, it will be in a terpolymer state including the rubber component).
ゴム成分が1重t%未満の場合には、得られた深絞構成
型品の開口部、ことにコツプの場合のリップ強度が不充
分で割れ易く実用上適さずさらに成形時の伸びも不充分
で生産効率が低下し不適当である。 また、30重量裂
を越えると気泡の連通化がおこり成形品が柔らかくなっ
て腰強度不足となり、また湯等を成形品に入れると泡が
発生して不適当であり、さらにゴム臭が強くなり、食品
用容器として汎用される深絞り容器成形用原反としては
不適当である。 通常、好ましい含有量は1〜20重量
%である。If the rubber component is less than 1% by weight, the opening of the resulting deep-drawn product, especially the lip in the case of a tap, will have insufficient strength and break easily, making it unsuitable for practical use, and furthermore, it will not elongate during molding. Even if it is sufficient, production efficiency decreases and it is inappropriate. In addition, if the weight exceeds 30, air bubbles become interconnected, making the molded product soft and lacking in stiffness.Additionally, if hot water or the like is poured into the molded product, bubbles will occur, making it unsuitable, and the smell of rubber will become stronger. , it is unsuitable as a raw material for forming deep-drawn containers, which are commonly used as food containers. Usually, the preferred content is 1 to 20% by weight.
一方、充填材は、成形品の外観向上、寸法精度、寸法安
定性等の点で効果を発揮する。 充填材の含有量が1重
量係未満では充分なガス量及び気泡の調整ができず成形
時の製品厚みのコントロールが不充分となり不適当であ
る。 20チを越えるとガス量及び気泡の調整はできる
が成形の際の原反の伸びが悪くなり不適当である。 通
常、好ましい含有量は4〜5重量%である。 かような
充填材としては、メルク、炭酸カルシウム、シラス、石
膏、カーボンブラック、ホワイトカーボン、炭酸マグネ
シウム、クレー、天然グイ酸等の一般無機充填材及び金
属粉等が挙けられる。On the other hand, fillers are effective in improving the appearance, dimensional accuracy, and dimensional stability of molded products. If the content of the filler is less than 1% by weight, the amount of gas and bubbles cannot be adjusted sufficiently, and the thickness of the product during molding cannot be controlled sufficiently, which is inappropriate. If it exceeds 20 inches, the gas amount and bubbles can be adjusted, but the elongation of the original fabric during molding becomes poor, which is inappropriate. Usually, the preferred content is 4 to 5% by weight. Examples of such fillers include general inorganic fillers such as Merck, calcium carbonate, shirasu, gypsum, carbon black, white carbon, magnesium carbonate, clay, natural guinic acid, and metal powder.
上記シート状発泡体の厚みは得られる複合シートの厚与
が1〜Btmttとなるよう調整される。 複合シート
の厚みが1M1以下の場合には他の条件を調節した際に
も深絞シの成形(ことに絞り比1以上のもの)が困難で
あり、3mgを越えると成形性特に成形品の側壁と底厚
みのバランスをとることが難しくなり不適当である。
ことに絞シ比の高い第2図のごときコツプのような容器
状成形品が従来に比して高効率で得られる点接合シート
としての厚へか2〜3Mとなるよう調整するのが好まし
い。The thickness of the sheet-like foam is adjusted so that the resulting composite sheet has a thickness of 1 to Btmtt. When the thickness of the composite sheet is less than 1M1, it is difficult to perform deep drawing even when other conditions are adjusted (particularly when the drawing ratio is 1 or more), and when it exceeds 3mg, the formability, especially the quality of the molded product, is difficult. It is difficult to balance the side wall and bottom thickness, making it inappropriate.
In particular, it is preferable to adjust the thickness to 2 to 3M as a point-bonded sheet that can be obtained with higher efficiency than conventional container-shaped molded products such as the pot shown in Figure 2, which has a high drawing ratio. .
このようなシート状発泡体は、種々の発泡剤を用いる所
謂押出発泡法により得ることができる。Such a sheet-like foam can be obtained by a so-called extrusion foaming method using various foaming agents.
発泡剤としては種々の揮発性発泡剤や分解型発泡剤が常
法で適用できる。 揮発性発泡剤としてハフロバン、ブ
タン、ペンタン等の沸点約−40℃〜45℃の炭化水素
、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、1,2−ジクロロテトラフルオロエタン等の沸
点約−47℃〜45℃のハロゲン化炭化水素及びこれら
の混合物等が適当である。 分解型発泡剤としては、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、4,4−オキシビス(ベンゼンスルホニルヒドラ
ジド)等の有機系発泡剤や、重炭酸ナトリウム又はクエ
ン酸のごとき有機酸もしくはその塩と重炭酸塩との組合
せ(ただし、これらはそれぞれ流動パラフィン等の被覆
剤で被覆されていてもよい)等が適当である。 場合に
よっては二酸化炭素、窒素ガス、水等も適用できる。
これらは常法により押出機内へ供給される。As the blowing agent, various volatile blowing agents and decomposable blowing agents can be used in a conventional manner. Volatile blowing agents include hydrocarbons with boiling points of about -40°C to 45°C, such as haflobane, butane, and pentane, and boiling points of about -47°C to 45°C, such as trichloromonofluoromethane, dichlorodifluoromethane, and 1,2-dichlorotetrafluoroethane. ℃ halogenated hydrocarbons and mixtures thereof are suitable. Examples of decomposable blowing agents include organic blowing agents such as azodicarbonamide, dinitrosopentamethylenetetramine, and 4,4-oxybis(benzenesulfonylhydrazide), and organic blowing agents such as sodium bicarbonate or citric acid or their salts. A combination with a carbonate (however, each of these may be coated with a coating agent such as liquid paraffin) is suitable. Depending on the case, carbon dioxide, nitrogen gas, water, etc. can also be applied.
These are fed into the extruder in a conventional manner.
ただし、上記シート状発泡体における発泡剤の残ガス量
は0.3モル/kg以下とする。 残ガス量が多いと二
次成形時の加熱による二次発泡が太きく、得られた成形
品の型の出が甘くなり不適当である。 好ましい残ガス
量は0.03〜0.8モル/穎である。 ことにシート
作成直後に残ガス量を0.03〜0.3モル/kgとな
るように発泡剤量等の押出条件を調整した場合に、熟成
なく同じラインで連続して二次成形を行なう同時成形(
インライン成形)が可能になり経済性等の点でより打首
しい。 なお、残カス量がシート作成直後に0.3モル
/kgを越える場合には、例えばシートを40〜50℃
に加熱してガス抜きを行なったり、ガス抜き時間を設定
する必要がある。However, the amount of residual gas of the blowing agent in the sheet-like foam is 0.3 mol/kg or less. If the amount of residual gas is large, secondary foaming due to heating during secondary molding will be large, and the resulting molded product will not come out easily, which is inappropriate. A preferable amount of residual gas is 0.03 to 0.8 mol/glume. In particular, if the extrusion conditions such as the amount of blowing agent are adjusted so that the amount of residual gas is 0.03 to 0.3 mol/kg immediately after sheet creation, secondary molding can be performed continuously on the same line without aging. Simultaneous molding (
In-line molding) becomes possible, making it more economical. In addition, if the amount of residual residue exceeds 0.3 mol/kg immediately after sheet production, the sheet may be heated at 40 to 50°C, for example.
It is necessary to heat the product to a certain temperature to degas it, or to set the degassing time.
上記のシート状発泡体の一面に非発泡樹脂フィルムを積
層することによりこの発明の深絞シ容器成形用ポリスチ
レン発泡シートが得られる。 非発泡樹脂フィルムとし
ては厚み5〜600μmの熱可塑性樹脂フィルムを用い
るのが適当である。The polystyrene foam sheet for forming deep-drawn containers of the present invention can be obtained by laminating a non-foamed resin film on one side of the above sheet-like foam. As the non-foamed resin film, it is appropriate to use a thermoplastic resin film with a thickness of 5 to 600 μm.
なお場合によっては両面にフィルムを積層してもよい。In some cases, films may be laminated on both sides.
上記熱可塑性樹脂フィルムの樹脂としては、ポリスチレ
ン、ポリエチレン、ポリスチレンとゴムとの混合又は共
重合物である耐衝撃性ポリスチレン、ポリプロピレン、
ポリエチレンテレフタレート等の一般にシート化できる
樹脂が挙げられ、これらのうち、ポリスチレン、高密度
ポリエチレン、耐衝撃性ポリスチレンが成形性の点で好
ましく、ポリスチレン及び耐衝撃性ポリスチレンが使い
易さの点でより好ましい。The resin of the thermoplastic resin film includes polystyrene, polyethylene, high-impact polystyrene which is a mixture or copolymer of polystyrene and rubber, polypropylene,
Examples include resins that can generally be made into sheets, such as polyethylene terephthalate. Among these, polystyrene, high-density polyethylene, and high-impact polystyrene are preferred in terms of moldability, and polystyrene and high-impact polystyrene are more preferred in terms of ease of use. .
上記フィルムの厚みが5μm未満では原反としての伸び
が悪く、さらに得られた成形品の機械的強度が低く不適
当である。 また、600μmを越えると成形後、打抜
くときリップ部の気泡がつぶされて連通となり、該フィ
ルムと前記シート状発泡体とが剥れる問題が発生しさら
に経済性の点で不利であり適さない。 第2図に示すご
とき成形品を作製する際の厚みとしては30〜500μ
mが通常好ましい。If the thickness of the film is less than 5 μm, it will not stretch well as a raw material, and the mechanical strength of the resulting molded product will be low, making it unsuitable. Moreover, if it exceeds 600 μm, the bubbles in the lip part will be crushed and communicated when punching out after molding, which will cause the problem of peeling of the film and the sheet-like foam, which is also disadvantageous in terms of economy, and is therefore not suitable. . The thickness when producing a molded product as shown in Figure 2 is 30 to 500μ.
m is usually preferred.
なお、上記熱可塑性樹脂フィルムの前記シート状発泡体
への積層は種々の方法で行なわれる。Note that the thermoplastic resin film may be laminated onto the sheet-like foam by various methods.
例えば、熱可塑性樹脂フィルムをシート状発泡体にダイ
内で積層する場合には、合流ダイ(例えばクロスへラド
ダイ)を用いて行なってもよく、ダイスリット手前、で
流入して積層を行なってもよい。For example, when laminating a thermoplastic resin film onto a sheet-like foam in a die, it may be carried out using a merging die (for example, a cross-to-ladder die), or it may be laminated by flowing in before the die slit. good.
また、シート状発泡体を押出発泡した後に積層する場合
には、熱可塑性樹脂フィルムの押出機を引取り機とを組
合せフィルムを押出して連続的に積層してもよく、予め
作製しておいた熱可塑性樹脂フィルムをシート状発泡体
に適宜積層することによって行なってもよい。 なお、
上記積層としては接着剤を使用することにより行なって
もよく、熱融着によって行なってもよい。 なお、接着
剤としては種々のものが使用できるが、ETA共重合体
などの酢酸ビニル系のものやBBHなどのゴム系のもの
が好適である。 これらの接着剤は溶剤タイプ、エマル
ジョンタイプ、フィルムタイプのいずれの形態で用いら
れてもよい。In addition, when laminating sheet-like foams after extrusion and foaming, it is also possible to combine a thermoplastic resin film extruder with a take-up machine to extrude the films and laminate them continuously. This may be carried out by appropriately laminating a thermoplastic resin film on a sheet-like foam. In addition,
The above-mentioned lamination may be performed by using an adhesive or by heat fusion. Note that various adhesives can be used, but vinyl acetate-based adhesives such as ETA copolymer and rubber-based adhesives such as BBH are preferred. These adhesives may be used in any form of solvent type, emulsion type, or film type.
このようにして得られたこの発明の深絞シ容器成形用ポ
リスチレン系発泡シートは、特定のシート状発泡体及び
特定の熱可塑性樹脂フィルムを用いた結合効果により深
絞シ容器状成形品を成形性良く簡便に得ることができ、
さらに従来の原反に比してその成形品生産効率は遥かに
向上しており大量生産用の成形用原反として極めて有用
なものである。The thus obtained polystyrene foam sheet for forming deep-drawn containers of the present invention can be used to form deep-drawn container-like molded products by the bonding effect using a specific sheet-like foam and a specific thermoplastic resin film. can be obtained easily and with good quality,
Furthermore, the production efficiency of molded products is much improved compared to conventional raw fabrics, making it extremely useful as a molding fabric for mass production.
以下、この発明の発泡シートを実施例により詳しく説明
する。Hereinafter, the foamed sheet of the present invention will be explained in detail with reference to Examples.
実施例
この発明の深絞り容器成形用ポリスチレン系発泡シート
のシート状発泡体のゴム分、充填材量。Examples Rubber content and amount of filler in the sheet-like foam of the polystyrene foam sheet for deep-drawn container molding of the present invention.
厚へ1発泡倍率を、及び非発泡樹脂フィルムのゴム分、
厚みを適宜変更したものを、口径106mg。1 foaming ratio to the thickness, and the rubber content of the non-foamed resin film,
The diameter is 106mg with the thickness changed appropriately.
深さ106ff肩、テーパー7度のコツプを、大きさ6
00X600gfflの上記発泡シートで16個取りで
きるように成形し、16個共技傷なしに得られたものを
、成形性○、内1個損傷受けたものを△、2個以上損傷
受けた場合×とした。 まfc得られたコツプを横にし
、上部よりリップ部に元の寸法の25チ圧縮をかけ、割
れなかった場合、リップワレ○、割れた場合×とした。Depth 106ff shoulder, taper 7 degree tip, size 6
The above foam sheet of 00 x 600gffl was molded so that 16 pieces could be made, and the 16 pieces obtained without any damage were evaluated as ○, △ if 1 of them was damaged, and × if 2 or more were damaged. And so. The obtained tip was laid on its side, and the original size of the lip was compressed by 25 inches from the top. If it did not crack, the lip crack was rated as ○, and if it cracked, it was rated as ×.
総合評価は成形性とりツブワレとで評価した。The overall evaluation was based on moldability and cracking.
第1表にその結果を比較例と共に示す。Table 1 shows the results along with comparative examples.
第1図は、この発明の深絞シ容器成形用ポリスチレン系
発泡シートを例示する断面図、第2図はこの発明のシー
トにより効率良く得られるコツプ状成形品を例示する斜
視図、第8図は、従来の成形用シートの型取りを示す模
式的平面説明図、第4図はこの発明のシートの型取りを
示す第3図相当図である。
(1)−・・深絞p成形用ポリスチレン系発泡シート、
(2)・・・シート状発泡体、
(3)・・・非発泡樹脂フィルム、
(4)・・・コツプ状成形品。FIG. 1 is a cross-sectional view illustrating a polystyrene foam sheet for forming deep-drawn containers of the present invention, FIG. 2 is a perspective view illustrating a pot-shaped molded product that can be efficiently obtained by the sheet of the present invention, and FIG. 8 FIG. 4 is a schematic plan explanatory view showing the molding of a conventional molding sheet, and FIG. 4 is a view corresponding to FIG. 3 showing the molding of the sheet of the present invention. (1)--polystyrene foam sheet for deep drawing p-forming,
(2)...Sheet-like foam, (3)...Non-foamed resin film, (4)...Cop-shaped molded product.
Claims (1)
体の少なくとも一面に非発泡樹脂フィルムを積層した厚
み1〜8Hの複合シートからなり、上記シート状発泡体
は基材樹脂に対して1〜30重量%相当のゴム成分及び
1〜20重量%相当の充填材を含有しかつ発泡剤の残ガ
ス量が0.8モル/kg以下に制御されたシート状発泡
体からなり、上記非発泡樹脂フィルムは厚与5〜600
μmの熱可塑性樹脂フィルムからなることを特徴とする
深絞シ容器成形用ポリスチレン系発泡シート。 2、非発泡樹脂フィルムの厚みが30〜500μmであ
る特許請求の範囲第1項記載の発泡シート。 8、発泡剤の残ガス量が0.08〜0.3モル/kgで
ある特許請求の範囲第1項記載の発泡シート。[Scope of Claims] 1. Consists of a composite sheet with a thickness of 1 to 8H, in which a non-foamed resin film is laminated on at least one side of a sheet-like foam whose base resin is polystyrene resin, and the sheet-like foam has a base material of polystyrene resin. From a sheet-like foam containing a rubber component equivalent to 1 to 30% by weight and a filler equivalent to 1 to 20% by weight based on the resin, and in which the residual gas amount of the blowing agent is controlled to 0.8 mol / kg or less The above non-foamed resin film has a thickness of 5 to 600
A polystyrene foam sheet for forming deep-drawn containers, characterized by being made of a μm thermoplastic resin film. 2. The foamed sheet according to claim 1, wherein the non-foamed resin film has a thickness of 30 to 500 μm. 8. The foamed sheet according to claim 1, wherein the amount of residual gas of the foaming agent is 0.08 to 0.3 mol/kg.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58057518A JPS59179633A (en) | 1983-03-31 | 1983-03-31 | Polystyrene sheet foam for forming deep-drawn container |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58057518A JPS59179633A (en) | 1983-03-31 | 1983-03-31 | Polystyrene sheet foam for forming deep-drawn container |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59179633A true JPS59179633A (en) | 1984-10-12 |
JPH0216690B2 JPH0216690B2 (en) | 1990-04-18 |
Family
ID=13057953
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58057518A Granted JPS59179633A (en) | 1983-03-31 | 1983-03-31 | Polystyrene sheet foam for forming deep-drawn container |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59179633A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6289743A (en) * | 1985-06-20 | 1987-04-24 | Eiwa Kasei Kogyo Kk | Production of styrene resin foam |
JP2003053911A (en) * | 2001-08-09 | 2003-02-26 | Kanegafuchi Chem Ind Co Ltd | Molded container comprising polystyrenic resin laminated foamed sheet |
JP2007210110A (en) * | 2006-02-07 | 2007-08-23 | Jsp Corp | Polystyrenic resin laminated sheet |
JP2010228182A (en) * | 2009-03-26 | 2010-10-14 | Sekisui Plastics Co Ltd | Polystyrene-based resin laminated foamed sheet and molded body |
CN102673074A (en) * | 2012-04-17 | 2012-09-19 | 芜湖市瑞诚工贸有限公司 | Plastic composite sheet for food cup |
CN102673069A (en) * | 2012-04-17 | 2012-09-19 | 芜湖市弘瑞包装制品有限公司 | High-strength plastic composite sheet for food cup |
JP2015182370A (en) * | 2014-03-25 | 2015-10-22 | 積水化成品工業株式会社 | Sheet for thermoforming, molding and container |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5973860B2 (en) * | 2012-09-28 | 2016-08-23 | 積水化成品工業株式会社 | Method for producing laminated foam sheet, method for producing foam molded article, and laminated foam sheet for thermoforming |
-
1983
- 1983-03-31 JP JP58057518A patent/JPS59179633A/en active Granted
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6289743A (en) * | 1985-06-20 | 1987-04-24 | Eiwa Kasei Kogyo Kk | Production of styrene resin foam |
JP2003053911A (en) * | 2001-08-09 | 2003-02-26 | Kanegafuchi Chem Ind Co Ltd | Molded container comprising polystyrenic resin laminated foamed sheet |
JP2007210110A (en) * | 2006-02-07 | 2007-08-23 | Jsp Corp | Polystyrenic resin laminated sheet |
JP2010228182A (en) * | 2009-03-26 | 2010-10-14 | Sekisui Plastics Co Ltd | Polystyrene-based resin laminated foamed sheet and molded body |
CN102673074A (en) * | 2012-04-17 | 2012-09-19 | 芜湖市瑞诚工贸有限公司 | Plastic composite sheet for food cup |
CN102673069A (en) * | 2012-04-17 | 2012-09-19 | 芜湖市弘瑞包装制品有限公司 | High-strength plastic composite sheet for food cup |
JP2015182370A (en) * | 2014-03-25 | 2015-10-22 | 積水化成品工業株式会社 | Sheet for thermoforming, molding and container |
Also Published As
Publication number | Publication date |
---|---|
JPH0216690B2 (en) | 1990-04-18 |
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