JPH0811149A - Heterogenous foamed sheet, production thereof and container - Google Patents

Heterogenous foamed sheet, production thereof and container

Info

Publication number
JPH0811149A
JPH0811149A JP6171559A JP17155994A JPH0811149A JP H0811149 A JPH0811149 A JP H0811149A JP 6171559 A JP6171559 A JP 6171559A JP 17155994 A JP17155994 A JP 17155994A JP H0811149 A JPH0811149 A JP H0811149A
Authority
JP
Japan
Prior art keywords
sheet
surface side
foaming
foamed
heterogeneous
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.)
Pending
Application number
JP6171559A
Other languages
Japanese (ja)
Inventor
Kiyohisa Kezuka
清壽 毛塚
Masaru Ishida
大 石田
Teruo Imai
輝夫 今井
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.)
Eneos Corp
Original Assignee
Nippon Petrochemicals 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 Nippon Petrochemicals Co Ltd filed Critical Nippon Petrochemicals Co Ltd
Priority to JP6171559A priority Critical patent/JPH0811149A/en
Publication of JPH0811149A publication Critical patent/JPH0811149A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To newly impart high rigidity, printability, beautifulness or the like while holding conventional characteristics, in a thermoplastic resin foamed sheet of which the foaming magnification is specific times or more and the density is a specific value or less, by differentiating the foaming state on one surface side of the sheet from that on the other surfaces side thereof. CONSTITUTION:A heterogenous foamed sheet S is characterized by that foaming magnification is 1.1 times or more and density is 0.8 or less and the foaming magnification on one surface side B of the sheet S is high while that on the other surface side A of the sheet is low or substantially zero. A foamed state is coarse on one surface side B of the sheet S and successively becomes dense toward the other surface side B thereof. By this constitution, the sheet S holds conventional characteristics such as lightweight properties, heat insulating properties or buffering properties on one surface side B thereof and can satisfy various physical properties such as rigidity, printability or beautifulness on the other surface side A thereof.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は一面側と他面側とで発泡
が異なった特殊な熱可塑性樹脂製発泡シートおよびその
製法・それを用いた容器に関し、好ましくは食品トレー
等の容器に用いられ、かつ自動車部材、建築部材・イン
テリア部材その他一般工業部材等の用途にも適用される
発泡シート・その製法・容器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a special thermoplastic resin foam sheet having different foaming on one side and the other side, a method for producing the same, and a container using the same, preferably used for containers such as food trays. The present invention relates to a foamed sheet, a method of manufacturing the same, and a container, which are also applied to applications such as automobile members, building members, interior members and other general industrial members.

【0002】[0002]

【従来の技術】従来、惣菜用トレー、弁当用容器等の食
品トレー用容器の発泡シートまたは自動車用内装材等に
使用されている発泡シートとしては、一般的には断面が
均一に発泡された発泡シート等が使用され、それら発泡
シートの製造方法として特開平4−364930号公報
や公表平1−50583号公報等が提案されている。こ
れらシートの発泡状態はシート全体が均等に発泡され、
保温性、緩衝性、軽量性等の諸物性が満足されている。
しかし、昨今における用途等の多様化に伴い、容器、建
築部材等においても、前記諸物性の他に、新たに高剛
性、印刷性、美麗性(表面平滑性)等の諸性状が要望さ
れている。
2. Description of the Related Art Conventionally, as a foamed sheet for a food tray container such as a side dish tray and a lunch box container or a foamed sheet used as an interior material for an automobile, the cross section is generally foamed uniformly. Foamed sheets and the like are used, and JP-A-4-364930 and JP-A-1-50583 have been proposed as methods for producing these foamed sheets. The foamed state of these sheets is that the entire sheet is foamed uniformly,
Various physical properties such as heat retention, cushioning, and lightness are satisfied.
However, with the recent diversification of uses and the like, various properties such as high rigidity, printability, and beauty (surface smoothness) have been newly demanded in addition to the above-mentioned physical properties in containers and building members. There is.

【0003】[0003]

【発明が解決しようとする課題】本発明の目的は、これ
ら従来技術の課題を解消し、軽量性、保温性、緩衝性、
断熱性等の従来の特性を保持し、かつ新たに高剛性、印
刷性、美麗性(表面平滑性)等を付与した不均質な発泡
シートおよびその製法・そのシートを用いた容器を提供
することを目的とする。
SUMMARY OF THE INVENTION The object of the present invention is to solve these problems of the prior art and to reduce the weight, the heat retaining property, the cushioning property,
To provide an inhomogeneous foamed sheet which retains the conventional properties such as heat insulating property and which is newly imparted with high rigidity, printability, beauty (surface smoothness), etc., a manufacturing method thereof, and a container using the sheet. With the goal.

【0004】[0004]

【課題を解決するための手段】本発明者らは上記の諸性
状が満足し得る特殊な発泡シートを開発するにあたり、
鋭意検討した結果、軽量性、保温性、緩衝性、断熱性等
の従来の特性を保持し、かつ新たに高剛性、印刷性、美
麗性(表面平滑性)等を付与した不均質な発泡シートお
よびその製法・そのシートを用いた容器を開発するに至
ったものである。
Means for Solving the Problems In developing a special foamed sheet satisfying the above various properties,
As a result of diligent study, a heterogeneous foamed sheet that retains the conventional properties such as light weight, heat retention, cushioning, and heat insulation properties, as well as newly added high rigidity, printability, beauty (surface smoothness), etc. And its manufacturing method and the development of a container using the sheet.

【0005】すなわち、本発明は、発泡倍率1.1倍以
上、比重が0.8以下である熱可塑性樹脂製発泡シート
であって、該シートの一面側と他面側とで発泡状態が異
なることを特徴とする不均質発泡シートにある。この不
均質発泡シートにあっては、発泡倍率が1.1〜40倍
であり、一面側Bと他面側Aの発泡セル径比B/Aが
1.2〜250倍であることが望ましい。また、熱可塑
性樹脂としてはポリオレフィンまたはその組成物が望ま
しく、発泡剤として不活性ガスを用いることが望まし
い。また、本発明は、発泡能を有する熱可塑性樹脂シー
トの供給手段と、該シートを加熱して不均質な発泡シー
トとする手段、該発泡シートの巻取手段を含むことを特
徴とする不均質発泡シートの製法である。さらに、本発
明は、上記した不均質発泡シートを用いたことを特徴と
する容器である。
That is, the present invention is a thermoplastic resin foam sheet having a foaming ratio of 1.1 times or more and a specific gravity of 0.8 or less, and the foaming state is different between one side and the other side of the sheet. A heterogeneous foam sheet characterized by the above. In this heterogeneous foamed sheet, it is desirable that the expansion ratio is 1.1 to 40 times and the foamed cell diameter ratio B / A on the one surface side B and the other surface side A is 1.2 to 250 times. . Further, polyolefin or a composition thereof is desirable as the thermoplastic resin, and it is desirable to use an inert gas as the foaming agent. Further, the present invention includes a means for supplying a thermoplastic resin sheet having a foaming ability, a means for heating the sheet to form an inhomogeneous foamed sheet, and a means for winding up the foamed sheet, which is characterized by being non-homogeneous. It is a method of manufacturing a foamed sheet. Furthermore, the present invention is a container characterized by using the above-mentioned heterogeneous foamed sheet.

【0006】以下、本発明を詳細に述べる。本発明で用
いる熱可塑性樹脂としては、特に制限はないものの、一
般的にはオレフィン系樹脂、エチレン−酢酸ビニル共重
合体ケン化物、ポリアミド系樹脂、ポリエステル系樹
脂、ポリカーボネート系樹脂、ポリ塩化ビニル系樹脂、
ポリスチレン系樹脂およびそれらの混合物等が挙げられ
る。
The present invention will be described in detail below. The thermoplastic resin used in the present invention is not particularly limited, but is generally an olefin resin, an ethylene-vinyl acetate copolymer saponified product, a polyamide resin, a polyester resin, a polycarbonate resin, a polyvinyl chloride resin. resin,
Examples thereof include polystyrene resins and mixtures thereof.

【0007】これらの中でもオレフィン系樹脂が好まし
く、具体的には、高・中密度ポリエチレン、高圧ラジカ
ル法低密度ポリエチレン、直鎖状低密度ポリエチレン、
超低密度ポリエチレン、エチレン−酢酸ビニル共重合
体、エチレン−(メタ)アクリル酸エチル共重合体等の
エチレン−(メタ)アクリル酸アルキルエステル共重合
体、ポリプロピレン、プロピレン−α−オレフィン共重
合体等が挙げられる。特に耐熱性、経済性等から好適な
例は、ポリエチレン系樹脂、ポリプロピレン系樹脂が挙
げられる。
Of these, olefin resins are preferable, and specifically, high / medium density polyethylene, high pressure radical method low density polyethylene, linear low density polyethylene,
Ultra low density polyethylene, ethylene-vinyl acetate copolymer, ethylene- (meth) acrylic acid alkyl ester copolymer such as ethylene- (meth) acrylic acid alkyl ester copolymer, polypropylene, propylene-α-olefin copolymer, etc. Is mentioned. Particularly preferable examples from the viewpoint of heat resistance and economy are polyethylene resins and polypropylene resins.

【0008】該ポリエチレン系樹脂としては(A)密度
0.86〜0.94g/cm3の高圧ラジカル重合法に
よる低密度ポリエチレンまたはエチレン−α−オレフィ
ン共重合体、(B)エチレンービニルエステル共重合
体、(C)エチレン−α,β−不飽和カルボン酸アルキ
ルエステル共重合体から選ばれた少なくとも1種または
その混合物が挙げられる。
Examples of the polyethylene resin include (A) low-density polyethylene or ethylene-α-olefin copolymer by a high-pressure radical polymerization method having a density of 0.86 to 0.94 g / cm 3 , and (B) ethylene-vinyl ester copolymer. At least one selected from a polymer and (C) ethylene-α, β-unsaturated carboxylic acid alkyl ester copolymer, or a mixture thereof can be mentioned.

【0009】より具体的には(A)密度0.86〜0.
94g/cm3の高圧ラジカル重合法による低密度ポリ
エチレンまたはエチレン−α−オレフィン共重合体とし
ては、ラジカル重合法による密度0.91〜0.94
g/cm3の低密度ポリエチレン(以下LDPEと略
す)および、チーグラー触媒等を用いる中低圧法及およ
びその他の公知の方法によるエチレンと炭素数3〜12
のα−オレフィンとの共重合体であり、密度0.86〜
0.91 g/cm3未満のエチレン−α−オレフィン
共重合体(超低密度ポリエチレン、以下VLDPEと略
す)および密度0.91〜0.94g/cm3のエチレ
ン−α−オレフィン共重合体(直鎖状低密度ポリエチレ
ン、以下LLDPEと略す)である。
More specifically, (A) density 0.86-0.
The low density polyethylene or ethylene-α-olefin copolymer produced by the high pressure radical polymerization method of 94 g / cm 3 has a density of 0.91 to 0.94 obtained by the radical polymerization method.
Low density polyethylene (hereinafter abbreviated as LDPE) of g / cm 3 and ethylene and carbon number 3 to 12 by the medium and low pressure method using Ziegler catalyst and other known methods
Of α-olefin and a density of 0.86 to
An ethylene-α-olefin copolymer having a density of less than 0.91 g / cm 3 (ultra-low density polyethylene, hereinafter abbreviated as VLDPE) and an ethylene-α-olefin copolymer having a density of 0.91 to 0.94 g / cm 3 ( Linear low-density polyethylene (hereinafter abbreviated as LLDPE).

【0010】ポリプロピレン系樹脂としては、プロピレ
ン単独重合体、プロピレンと他のα−オレフィンとのラ
ンダム、ブロック共重合体等が挙げられる。また、発泡
体の弾性体や剛性体を得るためには、これら樹脂を適宜
選択することが望ましい。例えば、高剛性を要求する場
合においては、プロピレン単独重合体を選択し、好まし
くはアイソタクシテイ(P0)が0.94以上であるこ
とが好ましい。また、発泡体の弾性を保持する場合には
該ポリプロピレン系樹脂にポリエチレン系樹脂を配合す
ることが好ましい。
Examples of polypropylene resins include propylene homopolymers, random copolymers of propylene and other α-olefins, and block copolymers. Further, in order to obtain an elastic body or a rigid body of foam, it is desirable to appropriately select these resins. For example, when high rigidity is required, a propylene homopolymer is selected, and the isotacticity (P 0 ) is preferably 0.94 or more. Further, when the elasticity of the foam is maintained, it is preferable to add a polyethylene resin to the polypropylene resin.

【0011】具体的なα−オレフィンとしては、炭素数
3〜12のプロピレン、1−ブテン、4−メチル−1−
ペンテン、1−ヘキセン、1−オクテン、1−ドデセン
等を挙げることができる。これらのうち好ましいのは1
−ブテン、4−メチル−1−ペンテン、1−ヘキセン、
1−オクテンである。エチレンと他のα−オレフィン共
重合体またはプロピレンと他のα−オレフィン共重合体
中のα−オレフィン含有量は5〜40モル%であること
が好ましい。
Specific α-olefins include propylene having 1 to 3 carbon atoms, 1-butene, and 4-methyl-1-.
Pentene, 1-hexene, 1-octene, 1-dodecene and the like can be mentioned. Of these, 1 is preferred
-Butene, 4-methyl-1-pentene, 1-hexene,
1-octene. The content of α-olefin in ethylene and other α-olefin copolymer or propylene and other α-olefin copolymer is preferably 5 to 40 mol%.

【0012】本発明におけるポリオレフィン組成物と
は、上記樹脂同志の混合物、樹脂とシリカ、タルク、炭
酸カルシウム等の無機または有機充填材、気泡調整剤、
滑剤、リン系酸化防止剤、フェノール系酸化防止剤、紫
外線防止剤、架橋剤、造核剤、難燃剤、顔料、染料等の
添加剤等の配合物を包含するものである。
The polyolefin composition in the present invention means a mixture of the above resins, a resin and an inorganic or organic filler such as silica, talc or calcium carbonate, a cell regulator,
It includes a mixture of additives such as a lubricant, a phosphorus-based antioxidant, a phenol-based antioxidant, a UV inhibitor, a crosslinking agent, a nucleating agent, a flame retardant, a pigment and a dye.

【0013】本発明で用いられる発泡剤としては、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、パラトルエンスルフォニルセミカルバジド、4,
4′−オキシビスベンゼンスルフォニルヒドラジド、ア
ゾビスイソブチロニトリル等の化学分解型発泡剤、トリ
フルオロメタン、モノクロロトリフルオロメタン、メチ
ルクロライド、ペンタン、ヘキサン等の揮発性発泡剤、
水(H2O)、炭酸ガス、一酸化炭素、ヘリウム、アル
ゴン、窒素、酸素、空気、フレオン、プロパン、ブタン
等のガス型発泡剤等、特に限定されるものではないが、
食品トレー等の容器として使用される場合には、窒素、
酸素、炭酸ガス、空気等の不活性ガス型発泡剤が好適で
ある。
As the foaming agent used in the present invention, azodicarbonamide, dinitrosopentamethylenetetramine, paratoluenesulfonyl semicarbazide, 4,
Chemical decomposition type foaming agents such as 4'-oxybisbenzenesulfonyl hydrazide and azobisisobutyronitrile, volatile foaming agents such as trifluoromethane, monochlorotrifluoromethane, methyl chloride, pentane and hexane,
Gas type blowing agents such as water (H 2 O), carbon dioxide, carbon monoxide, helium, argon, nitrogen, oxygen, air, freon, propane and butane are not particularly limited.
When used as a container for food trays, etc., nitrogen,
Inert gas type blowing agents such as oxygen, carbon dioxide and air are suitable.

【0014】以下、本発明を図面で詳述する。図1は本
発明の不均質発泡シートの一例の断面模式図であり、同
図において、不均質発泡シートSは、発泡倍率1.1倍
以上、比重が0.8以下で、一面側Bが発泡倍率が高
く、他面側Aが発泡倍率が低いか、もしくは実質的に発
泡していない状態の発泡シートであることが肝要であ
り、一面側Bから他面側Aに向かって順次発泡状態が粗
から密になっていることが望ましい。しかしながら、図
2に示すように使用目的によっては、シートSの一面側
B′から他面側A′の1/5程度、好ましくは1/4程
度までは発泡状態はほぼ均一であってもよい。また、樹
脂の種類により異なるが、食品トレー等においては、発
泡倍率は1.1〜40倍、好ましくは1.1〜30倍、
さらに好ましく1.1〜20倍であることが望ましい。
このような構成とすることにより、一面側Bは、軽量
性、保温性、緩衝性、断熱性等の従来の特性を保持し、
他面側Aは剛性、印刷性、美麗性(表面平滑性)等の諸
物性を満足することが可能となる。
The present invention will be described in detail below with reference to the drawings. FIG. 1 is a schematic cross-sectional view of an example of the heterogeneous foamed sheet of the present invention. In the figure, the heterogeneous foamed sheet S has a foaming ratio of 1.1 times or more, a specific gravity of 0.8 or less, and one surface side B It is important that the expansion sheet has a high expansion ratio and the other surface side A has a low expansion ratio or is a substantially non-foamed state, and the foaming state is sequentially from the one surface side B to the other surface side A. It is desirable that the is coarse to dense. However, as shown in FIG. 2, depending on the purpose of use, the foamed state may be substantially uniform from one side B'of the sheet S to about 1/5, preferably about 1/4 of the other side A '. . Further, although depending on the type of resin, in a food tray or the like, the expansion ratio is 1.1 to 40 times, preferably 1.1 to 30 times,
It is more preferably 1.1 to 20 times.
With such a configuration, the one side B retains the conventional characteristics such as light weight, heat retention, cushioning, and heat insulation,
The other surface A can satisfy various physical properties such as rigidity, printability, and beauty (surface smoothness).

【0015】本発明の不均質発泡シートの厚みは、建築
土木資材、自動車部材、食品資材等の用途、使用目的等
により異なり特に限定されないが、例えば惣菜トレー等
の食品トレー用の容器については、不活性ガスを使用し
た数ミリ程度の薄物シートとすることが望ましい。
The thickness of the heterogeneous foamed sheet of the present invention varies depending on the application and purpose of use of building civil engineering materials, automobile parts, food materials, etc., and is not particularly limited. For example, for containers for food trays such as side dish trays, It is desirable to make a thin sheet of about several millimeters using an inert gas.

【0016】また本発明の発泡セルの大きさは、発泡状
態が高い一面側Bからシート全体の厚さに対して20%
までが10〜500μmの範囲、発泡状態の低い他面側
Aからシート全体の厚さに対して20%までがソリッド
状態から200μmの範囲が望ましく、特に一面側Bと
他面側Aの比がB/A=1.2〜250、好ましくは2
0から100の範囲であることが望ましい。該比が1.
2未満では本発明の発泡シートの特徴が発揮されず、2
50を超える場合には剛性の低下等の虞を生ずる。
The size of the foamed cell of the present invention is 20% of the total thickness of the sheet from the one side B where foaming is high.
Is in the range of 10 to 500 μm, and it is desirable that 20% of the total thickness of the sheet from the other side A having a low foaming state to the solid state is 200 μm. In particular, the ratio between the one side B and the other side A is B / A = 1.2 to 250, preferably 2
It is preferably in the range of 0 to 100. The ratio is 1.
If it is less than 2, the characteristics of the foamed sheet of the present invention are not exhibited, and 2
When it exceeds 50, there is a possibility that the rigidity is lowered.

【0017】本発明の不均質発泡シートの製法とは、
発泡能を有する熱可塑性樹脂シートの供給手段と、該
シートを加熱して不均質な発泡シートとする手段、該
発泡シートの巻取手段を含むことを特徴とする不均質発
泡シートの製造方法である。上記本発明の発泡能を有す
る熱可塑性樹脂シートとは、加熱により発泡剤がいまだ
発泡能力を有するシートを意味するものである。
The manufacturing method of the heterogeneous foam sheet of the present invention is
A method for producing a heterogeneous foamed sheet, comprising: a means for supplying a thermoplastic resin sheet having foaming ability; a means for heating the sheet to form an inhomogeneous foamed sheet; and a means for winding the foamed sheet. is there. The thermoplastic resin sheet having a foaming ability of the present invention means a sheet in which the foaming agent still has a foaming ability by heating.

【0018】以下、本発明の不均質発泡シートの製法の
一例を図面に基づいて詳述する。図3は本発明の不均質
発泡シートの製法の概略工程図を示したものである。同
図において、発泡能を有する熱可塑性樹脂シートの供
給手段とは、1は樹脂原料を供給するホッパー、2は押
出機、3は不活性ガスの導入または不要ガスの排気用ベ
ント口、4はTダイ等からなる熱可塑性樹脂原料の供給
工程および/または発泡剤の供給工程と、5は挟圧ロー
ル、6は冷媒液槽、7は水、油、ポリエチレングリコー
ル等を使用した冷媒液、8,8′はターンロール、9は
油圧機構、ラックとピニオンによる機構、ネジ機構等に
よる駆動可能な上下調整駆動機構等を包含した溶融熱可
塑性樹脂の冷却工程を包含するものであり、該シート
を加熱して不均質な発泡シートとする手段とは、赤外ヒ
ーター11等を具備したオーブン装置12と冷却ロール
15,15′、冷却水槽等(図示せず)の冷却工程とか
ら構成されるが、所望により該発泡シートの反り等を解
消するアニール工程(図示せず)、圧延工程(図示せ
ず)等を包含するものである。また、該発泡シートの
巻取手段とは、18は巻取ロール等を具備する巻取手段
を示したもので所望により巻取る前の発泡シートの表面
に予めコロナ放電処置装置17等を施す表面処理工程、
印刷工程(図示せず)、接着剤の塗工工程(図示せず)
等を包含するものである。
An example of the method for producing the heterogeneous foamed sheet of the present invention will be described in detail below with reference to the drawings. FIG. 3 shows a schematic process diagram of the method for producing a heterogeneous foamed sheet of the present invention. In the figure, the supplying means of the thermoplastic resin sheet having the foaming ability is as follows: 1 is a hopper for supplying a resin raw material, 2 is an extruder, 3 is a vent port for introducing an inert gas or exhausting unnecessary gas, 4 is a A step of supplying a thermoplastic resin raw material and / or a step of supplying a foaming agent, such as a T-die, 5 is a pressing roll, 6 is a refrigerant liquid tank, 7 is a refrigerant liquid using water, oil, polyethylene glycol, or the like, 8 , 8'is a turn roll, 9 is a cooling mechanism of a molten thermoplastic resin including a hydraulic mechanism, a mechanism by a rack and pinion, a vertical adjustment drive mechanism that can be driven by a screw mechanism, etc. The means for heating to make an inhomogeneous foamed sheet includes an oven device 12 equipped with an infrared heater 11 and the like, cooling rolls 15 and 15 ', and a cooling step of a cooling water tank or the like (not shown). , Place (Not shown) annealing step to eliminate such warpage of the foam sheet is intended to encompass rolling step (not shown) or the like. Further, the foaming sheet winding means 18 is a winding means provided with a winding roll or the like, and a surface to which a corona discharge treatment device 17 or the like is preliminarily applied to the surface of the foamed sheet before winding if desired. Processing steps,
Printing process (not shown), adhesive coating process (not shown)
Etc. are included.

【0019】以下、本発明の一例を示す。該熱可塑性樹
脂の供給工程および/または発泡剤の供給工程とは、発
泡剤として分解型発泡剤の場合には、該熱可塑性樹脂ペ
レットと化学分解型発泡剤をドライブレンドしてホッパ
ー1に供給し、押出機2内で樹脂の融点以上、発泡剤の
実質分解しない温度で均一に溶融溶解させる。また、発
泡剤として不活性ガス等のような場合には押出機のベン
ト口3から該ガスを導入して、押出機内で樹脂の融点以
上、発泡剤の実質分解しない温度で均一に溶融収着さ
せ、次いで押出機先端のTダイ4から実質的に発泡して
いない溶融樹脂シートを押出し、次いで、押出された溶
融樹脂シートは冷却工程でTダイ4出口で急冷され、発
泡剤の発泡を抑制制御してシート化される。
An example of the present invention will be shown below. In the case of a decomposable foaming agent as the foaming agent, the thermoplastic resin supplying step and / or the foaming agent supplying step means dry blending the thermoplastic resin pellets and the chemically decomposable foaming agent and supplying them to the hopper 1. Then, in the extruder 2, it is melted and melted uniformly at a temperature not lower than the melting point of the resin and at which the foaming agent is not substantially decomposed. When an inert gas or the like is used as the foaming agent, the gas is introduced from the vent port 3 of the extruder to uniformly melt and sorb the gas in the extruder at a temperature not lower than the melting point of the resin and at which the foaming agent is not substantially decomposed. Then, the molten resin sheet that is not substantially foamed is extruded from the T die 4 at the tip of the extruder, and then the extruded molten resin sheet is rapidly cooled at the outlet of the T die 4 in the cooling step to suppress foaming of the foaming agent. It is controlled and made into a sheet.

【0020】該冷却工程においては、Tダイ4より吐出
された溶融樹脂シートをダイ直下に設置された一対の挟
圧ロール5に導入する。該挟圧ロールは、冷媒液槽6内
に設置され、ロール5の全部または一部を冷媒液7に浸
漬するようにして装備されている。挟圧ロールの全部ま
たは一部を冷媒液に浸漬するのは該ロールが溶融樹脂に
よって加熱されるのを防止するためである。
In the cooling step, the molten resin sheet discharged from the T die 4 is introduced into a pair of pinching rolls 5 installed immediately below the die. The pinching roll is installed in the coolant liquid tank 6 and is equipped so that the roll 5 is wholly or partially immersed in the coolant liquid 7. The whole or part of the pinching roll is immersed in the refrigerant liquid in order to prevent the roll from being heated by the molten resin.

【0021】Tダイ4出口と挟圧ロール5の間を可能な
限り近接させるために、冷媒液槽6は上下調整駆動機構
9によりTダイ4出口と挟圧ロール5の間を調整され
る。また、成形速度が高速化した場合は挟圧ロールに冷
媒液を巻き込みシートに冷却ムラを生じることあるが、
この時は数段の水切りロール(図示せず)と組み合わせ
るのが有効である。こうすることによって、Tダイ4よ
り吐出された高温度のシートは溶融状態で挟圧ロール5
に導入されて表面が平滑化された後に冷媒液7中で冷却
され、さらにロール群を通過させることによりシート全
体の反りやひずみの修正された良好な未発泡樹脂シート
10(発泡能を有するシート)を効率的に成形すること
が可能である。
In order to bring the outlet of the T die 4 and the pinching roll 5 as close to each other as possible, the refrigerant liquid tank 6 is adjusted between the outlet of the T die 4 and the pinching roll 5 by the vertical adjustment drive mechanism 9. In addition, when the molding speed is increased, the refrigerant liquid may be entangled in the pinching roll to cause uneven cooling of the sheet,
At this time, it is effective to combine with several stages of draining rolls (not shown). By doing so, the high temperature sheet discharged from the T-die 4 is in a molten state in the pressing roller 5
Of the non-foamed resin sheet 10 (a sheet having a foaming ability) in which the surface is smoothed and then cooled in the refrigerant liquid 7, and the warp and strain of the entire sheet are corrected by passing through the roll group. ) Can be efficiently molded.

【0022】上記で製造された発泡能を有するシート1
0は、赤外線ヒーター11を具備したオーブン装置12
内に導入され、一面側Bが加熱発泡される。好ましくは
一面側Bから他面側Aに向かって順次発泡状態が密にな
るように発泡させることが望ましいが、使用目的によっ
ては、シート10の一面側Bから他面側Aの1/4程
度、好ましくは1/3程度までは発泡状態が均一になる
ように発泡させてもよい。また、加熱手段は特に限定さ
れるものではなく、樹脂の種類、組成、配合、あるいは
使用目的、用途により異なるが、加熱温度、加熱時間を
適宜選択するために、赤外線ヒーター12の代わりに、
バーナー、熱板、熱ロール、熱ベルト、加熱蒸気、熱風
等を単独または併用して使用してもよい。
The sheet 1 having the foaming ability manufactured as described above
0 is an oven device 12 equipped with an infrared heater 11.
It is introduced into the inside and the one side B is heated and foamed. It is desirable to foam so that the foaming state becomes denser from the one surface side B to the other surface side A sequentially, but depending on the purpose of use, about 1/4 of the one surface side B to the other surface side A of the sheet 10 Alternatively, the foaming may be performed until the foaming state becomes uniform up to about 1/3. Further, the heating means is not particularly limited, and varies depending on the type, composition, blending, or purpose of use, application of the resin, but in order to appropriately select the heating temperature and the heating time, instead of the infrared heater 12,
A burner, hot plate, hot roll, hot belt, heated steam, hot air, etc. may be used alone or in combination.

【0023】また、オーブン装置12を出た後は、一対
の冷却ロール15,15′で冷却しながら最終的にシー
トの反り等を矯正するためにアニール工程(図示せず)
を経て、所望により、コロナ放電処理、接着剤塗工工程
等を経て巻取り、製品とするものである。
After leaving the oven device 12, an annealing process (not shown) is performed to finally correct the warp of the sheet while cooling it with a pair of cooling rolls 15 and 15 '.
Then, if desired, the product is wound up through a corona discharge treatment, an adhesive coating process, etc. to obtain a product.

【0024】本発明の容器とは、上記した不均質シート
を用いた容器であり、ポリオレフィン系樹脂またはその
組成物からなるものが好ましく、特に食品用容器におい
ては、保温性、耐熱性、剛性等の点からポリプロピレン
系樹脂で構成され、かつ発泡剤として不活性ガスを用い
たものが好ましい。
The container of the present invention is a container using the above-mentioned heterogeneous sheet, and is preferably made of a polyolefin resin or its composition. Particularly, in the case of food containers, heat retention, heat resistance, rigidity, etc. From this point, it is preferable to use a polypropylene resin and use an inert gas as the foaming agent.

【0025】本発明の容器とは、生鮮食品用トレー、惣
菜用トレー、弁当箱、茸用トレー等のトレー類、ラーメ
ンカップ等のカップ類等の食品用容器、断熱容器、魚箱
等を包含するものであり、熱成形、絞り成形、プレス成
形等で成形される。また、前記発泡能を有するシートを
直接熱成形等の容器成形時に発泡させてもよい。
The containers of the present invention include trays such as fresh food trays, side dish trays, lunch boxes, and trays for mushrooms, food containers such as cups such as ramen cups, heat-insulating containers, and fish boxes. And is formed by thermoforming, drawing, press forming, or the like. Further, the sheet having the foaming ability may be directly foamed at the time of molding a container such as thermoforming.

【0026】また本発明の容器では、内面を発泡状態を
粗とし外面を密とする構造、内面を密とし、外面を粗と
する構造としてもよいが、一般的には内面を発泡状態を
粗とし、外面を密とする構造が、印刷が外面にできる
こと、外面が美麗性(平滑性)等を有することから好
ましい。
In the container of the present invention, the inner surface may have a foamed state and the outer surface may have a dense structure, or the inner surface may have a dense structure and the outer surface may have a rough structure. The structure in which the outer surface is dense is preferable because printing can be performed on the outer surface and the outer surface has beauty (smoothness).

【0027】本発明においては、本発明の要旨を逸脱し
ない範囲で、架橋剤、酸化防止剤、紫外線吸収剤、顔料
等の添加剤を配合してもよい。
In the present invention, additives such as a crosslinking agent, an antioxidant, an ultraviolet absorber and a pigment may be blended within the range not departing from the gist of the present invention.

【0028】[0028]

【実施例】以下、本発明を実施例で詳述する。実施例1 図3の装置を用いて、樹脂としてポリプロピレン樹脂
(MFR=0.5g/10分、密度=0.90g/cm
3、商品名:日石ポリプロ E610G、日本石油化学
(株)製)をホッパー1から押出機に導入し、発泡剤と
してN2ガスをベント口3よりフイードし、成形速度5
m/分、厚さ2mmで押出し、温度27℃の冷媒液
(水)槽に導入し、実質的に未発泡のシートを得た。次
いで、該シートを特殊ガスバーナーと赤外線ヒーター
(1.9KW、280mm×3本)を具備したオーブン
装置で片面発泡させて本発明の不均質発泡シートを製造
し、評価した結果、平均発泡倍率1.8倍、A面から2
0%の厚みまでのセル径(反射型電子顕微鏡SEM J
EOL製JSM−T20で測定)が平均5μmであり、
B面から20%の厚みまでのセル径が150μmであ
り、B/A=30であった。このシートを用いてB面を
内側としてトレーを成形したところ、外面が非常に平滑
で、かつ印刷特性も良好であった。
EXAMPLES The present invention will be described in detail below with reference to examples. Example 1 Using the apparatus of FIG. 3, polypropylene resin (MFR = 0.5 g / 10 min, density = 0.90 g / cm) was used as the resin.
3 , product name: Nisseki Polypro E610G, manufactured by Nippon Petrochemical Co., Ltd.) was introduced into the extruder from the hopper 1, N 2 gas as a foaming agent was fed through the vent port 3, and the molding speed was 5
The sheet was extruded at a temperature of 27 ° C. at a temperature of 27 ° C. to obtain a substantially unfoamed sheet. Next, the sheet was foamed on one side with an oven equipped with a special gas burner and an infrared heater (1.9 kW, 280 mm × 3) to produce the heterogeneous foamed sheet of the present invention, and the evaluation revealed that the average foaming ratio was 1 .8 times, 2 from side A
Cell diameter up to 0% thickness (reflection electron microscope SEM J
Is 5 μm on average, measured by ESM JSM-T20,
The cell diameter from the B surface to the thickness of 20% was 150 μm, and B / A = 30. When a tray was formed using this sheet with the side B as the inside, the outside was very smooth and the printing characteristics were good.

【0029】実施例2 図3の装置を用いて、樹脂としてポリプロピレン樹脂
(MFR=0.5g/10分、密度=0.90g/cm
3、商品名:日石ポリプロ E610G、日本石油化学
(株)製)をホッパー1から押出機に導入し、発泡剤と
してN2ガスをベント口3よりフイードし、成形速度3
m/分、厚さ4mmで押出し、温度27℃の冷媒液
(水)槽に導入し、実質的に未発泡のシートを得た。次
いで、該シートを特殊ガスバーナーと赤外線ヒーター
(1.9KW、280mm×3本)を具備したオーブン
装置で片面発泡させて本発明の不均質発泡シートを製造
し、評価した結果、平均発泡倍率15倍、A面から20
%の厚みまでのセル径(反射型電子顕微鏡SEM JE
OL製JEM−T20で測定)が平均5μmであり、B
面から20%の厚みまでのセル径が210μmであり、
B/A=42であった。このシートを用いてB面を内側
としてトレーを成形したところ、外面が非常に平滑で、
かつ印刷特性も良好であった。
Example 2 Using the apparatus of FIG. 3, polypropylene resin (MFR = 0.5 g / 10 min, density = 0.90 g / cm) was used as the resin.
3 , the product name: Nisseki Polypro E610G, manufactured by Nippon Petrochemical Co., Ltd.) was introduced into the extruder from the hopper 1, N 2 gas as a foaming agent was fed through the vent port 3, and the molding speed was 3
The sheet was extruded at a temperature of 27 ° C. at a temperature of 27 ° C. to obtain a substantially unfoamed sheet. Then, the sheet was foamed on one side in an oven equipped with a special gas burner and an infrared heater (1.9 kW, 280 mm × 3) to produce a heterogeneous foamed sheet of the present invention, which was evaluated. 20 times from side A
% Cell diameter (reflection electron microscope SEM JE
(Measured by JEM-T20 manufactured by OL) is 5 μm on average, and B
The cell diameter from the surface to the thickness of 20% is 210 μm,
B / A = 42. When a tray was formed using this sheet with the B side as the inner side, the outer surface was very smooth and
The printing characteristics were also good.

【0030】[0030]

【発明の効果】本発明は発泡状態が高い一面側Bと発泡
状態の低い他面側Aとで発泡状態が異なった特殊な熱可
塑性樹脂製発泡シートとすることにより、一面側Bは軽
量性、保温性、緩衝性、断熱性等の従来の特性を保持
し、他面側Aは剛性、印刷性、美麗性(表面平滑性)等
の諸物性を満足することが可能となり、食品トレー等の
容器、自動車部材、建築部材・インテリア部材その他一
般工業部材等の用途にも適用される。
EFFECTS OF THE INVENTION According to the present invention, the one side B is lightweight because the one side B having a high degree of foaming and the other side A having a low degree of foaming have different foaming states made of a special thermoplastic resin. , Other properties such as rigidity, printability, beauty (surface smoothness), etc. can be satisfied on the other side A while maintaining the conventional characteristics such as heat retention, cushioning and heat insulation. It is also applied to applications such as containers, automobile parts, building parts / interior parts, and other general industrial parts.

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

【図1】 本発明の不均質発泡シートの一例の断面模式
図。
FIG. 1 is a schematic sectional view of an example of a heterogeneous foam sheet of the present invention.

【図2】 本発明の不均質発泡シートの他の例の断面模
式図。
FIG. 2 is a schematic sectional view of another example of the heterogeneous foamed sheet of the present invention.

【図3】 本発明の不均質発泡シートの製法の概略工程
図。
FIG. 3 is a schematic process diagram of a method for producing a heterogeneous foam sheet of the present invention.

【符号の説明】[Explanation of symbols]

S:不均質発泡シート、A,A′:他面側、B,B′:
一面側、1:ホッパー、2:押出機、3:ベント口、
4:Tダイ、5:挟圧ロール、6:冷却液槽、7:冷却
液、8,8′:ターンロール、9:上下調整駆動機構、
10:発泡能シート、11:赤外線ヒーター、12:オ
ーブン装置、13,13′:ロール、14,14′:ロ
ール、15,15′:冷却ロール、16:ロール、1
7:コロナ放電装置、18:巻取ロール。
S: Heterogeneous foamed sheet, A, A ': other side, B, B':
One side, 1: Hopper, 2: Extruder, 3: Vent port,
4: T die, 5: pinching roll, 6: cooling liquid tank, 7: cooling liquid, 8, 8 ': turn roll, 9: vertical adjustment drive mechanism,
10: Foaming ability sheet, 11: Infrared heater, 12: Oven device, 13, 13 ': Roll, 14, 14': Roll, 15, 15 ': Cooling roll, 16: Roll, 1
7: Corona discharge device, 18: winding roll.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29L 7:00 C08L 23:02 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification number Agency reference number FI Technical display location B29L 7:00 C08L 23:02

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 発泡倍率1.1倍以上、比重が0.8以
下である熱可塑性樹脂製発泡シートであって、該シート
の一面側と他面側とで発泡状態が異なることを特徴とす
る不均質発泡シート。
1. A thermoplastic resin foam sheet having a foaming ratio of 1.1 times or more and a specific gravity of 0.8 or less, wherein one surface side and the other surface side of the sheet have different foaming states. Inhomogeneous foam sheet.
【請求項2】 前記不均質発泡シートの発泡倍率が、
1.1〜40倍であり、一面側Bと他面側Aの発泡セル
径比(B/A)が1.2〜250倍であることを特徴と
する請求項1に記載の不均質発泡シート。
2. The expansion ratio of the heterogeneous foam sheet is
It is 1.1 to 40 times, and the foam cell diameter ratio (B / A) of the one surface side B and the other surface side A is 1.2 to 250 times, and the heterogeneous foaming according to claim 1. Sheet.
【請求項3】 前記熱可塑性樹脂がポリオレフィンまた
はその組成物であることを特徴とする請求項1または2
記載の不均質発泡シート。
3. The thermoplastic resin according to claim 1, wherein the thermoplastic resin is a polyolefin or a composition thereof.
The heterogeneous foamed sheet described.
【請求項4】 発泡剤として不活性ガスを用いたことを
特徴とする請求項1〜3のいずれかに記載の不均質発泡
シート。
4. The heterogeneous foamed sheet according to claim 1, wherein an inert gas is used as the foaming agent.
【請求項5】 発泡能を有する熱可塑性樹脂シートの供
給手段と、該シートを加熱して不均質な発泡シートとす
る手段、該発泡シートの巻取手段を含むことを特徴とす
る不均質発泡シートの製法。
5. A non-homogeneous foam comprising: a means for supplying a thermoplastic resin sheet having foaming ability; a means for heating the sheet to form a non-homogeneous foam sheet; and a means for winding the foam sheet. How to make a sheet.
【請求項6】 請求項1〜4のいずれかに記載の不均質
発泡シートを用いたことを特徴とする容器。
6. A container using the heterogeneous foamed sheet according to claim 1.
JP6171559A 1994-07-01 1994-07-01 Heterogenous foamed sheet, production thereof and container Pending JPH0811149A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6171559A JPH0811149A (en) 1994-07-01 1994-07-01 Heterogenous foamed sheet, production thereof and container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6171559A JPH0811149A (en) 1994-07-01 1994-07-01 Heterogenous foamed sheet, production thereof and container

Publications (1)

Publication Number Publication Date
JPH0811149A true JPH0811149A (en) 1996-01-16

Family

ID=15925388

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6171559A Pending JPH0811149A (en) 1994-07-01 1994-07-01 Heterogenous foamed sheet, production thereof and container

Country Status (1)

Country Link
JP (1) JPH0811149A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11201379A (en) * 1998-01-13 1999-07-30 Sanyo Electric Co Ltd Vacuum heat insulating material and manufacture thereof
US6685875B2 (en) 2000-04-28 2004-02-03 Sumitomo Chemical Company, Ltd. Foamed thermoplastic resin molding and process for producing the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11201379A (en) * 1998-01-13 1999-07-30 Sanyo Electric Co Ltd Vacuum heat insulating material and manufacture thereof
US6685875B2 (en) 2000-04-28 2004-02-03 Sumitomo Chemical Company, Ltd. Foamed thermoplastic resin molding and process for producing the same

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