JPS606431A - Manufacture of cylindrical laminated film - Google Patents

Manufacture of cylindrical laminated film

Info

Publication number
JPS606431A
JPS606431A JP58114308A JP11430883A JPS606431A JP S606431 A JPS606431 A JP S606431A JP 58114308 A JP58114308 A JP 58114308A JP 11430883 A JP11430883 A JP 11430883A JP S606431 A JPS606431 A JP S606431A
Authority
JP
Japan
Prior art keywords
crystalline thermoplastic
thermoplastic resin
outer layer
inner layer
layer
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
Application number
JP58114308A
Other languages
Japanese (ja)
Other versions
JPH0261376B2 (en
Inventor
Masakatsu Kimura
正克 木村
Osamu Nakamura
中村 収
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical 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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP58114308A priority Critical patent/JPS606431A/en
Publication of JPS606431A publication Critical patent/JPS606431A/en
Publication of JPH0261376B2 publication Critical patent/JPH0261376B2/ja
Granted legal-status Critical Current

Links

Classifications

    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9115Cooling of hollow articles
    • B29C48/912Cooling of hollow articles of tubular films
    • B29C48/913Cooling of hollow articles of tubular films externally
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils

Abstract

PURPOSE:To produce a cylindrical laminated film that is free from curl and excellent in transparency, by using crystalline thermoplastic resins that can provide a special relationship between an inner layer and an outer layer, and performing down-flow water-cooled inflation forming. CONSTITUTION:As a crystalline thermoplastic resin for an inner layer is used a resin having a melting point relatively higher, preferably 5 deg.C or more higher, than the crystalline thermoplastic resin for an outer layer. The resin for the inner layer, the resin for the outer layer and, if required, various additives are fed to an extruder 1, and after they are melted and mixed, they are introduced into a circular and a die 2. Then they are extruded downward and is subjected to down-flow water-cooled inflation forming (for example, blowing is effected by an air ring 3 and cooling water 4 is directly brought in contact with the bulb). The cooling temperature is 10-40 deg.C, and the blow-up ratio is 0.8-3. The layer thickness ratio of the outer layer to the inner layer is to be in the range of 30:70- 97:3.

Description

【発明の詳細な説明】 本発明は筒状積層フィルムの製造方法に関し、さらに詳
しくは透明性にすぐれるとともにカールを防止した筒状
積層フィルムの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a cylindrical laminate film, and more particularly to a method for manufacturing a cylindrical laminate film that has excellent transparency and prevents curling.

従来、低密度ポリエチレン樹脂、ポリプロピレン樹脂な
どは機械的性質や透明性などがすぐれているため、多く
の分野で用いられている。
Conventionally, low-density polyethylene resins, polypropylene resins, and the like have been used in many fields because of their excellent mechanical properties and transparency.

しかしながら、これら結晶性熱可塑性樹脂から得られる
筒状フィルムは通常の上吹き空、冷インクレージョン成
形で製造した場合、透明性が十分でなく、その用途は大
巾に制限されている。そのため、下吹き水冷インフレー
ション成形によって溶融樹脂膜を急冷することが試みら
れている。しかしながら、透明性を向上させるために急
冷効果を利用すればするほど、溶融樹脂膜の内外の冷却
差が生じ、内側に大きくカールを生じるとともにブロッ
キングを生じ、フィルム製品としては利用することがで
きなくなるという問題がある。特に近時注目されている
直鎮状低密度ポリエチレンにあっては透明性にすぐれ、
しかもカールやブロッキングなどが生じないフィルムは
未だ得られていない。他方、積層フィルムにおいて成形
収縮率のより大きい樹脂側に固体充填剤を配合する方法
も提案されているが、この方法はカール防止には効果的
であるが、透明性の要求を満足できないという欠点があ
る。
However, when the cylindrical films obtained from these crystalline thermoplastic resins are produced by conventional top-blown air or cold ink injection molding, they do not have sufficient transparency, and their uses are largely limited. Therefore, attempts have been made to rapidly cool the molten resin film by bottom-blown water-cooled inflation molding. However, the more the rapid cooling effect is used to improve transparency, the more a difference in cooling between the inside and outside of the molten resin film occurs, causing large curls on the inside and blocking, making it impossible to use it as a film product. There is a problem. In particular, straight-lined low-density polyethylene, which has been attracting attention recently, has excellent transparency.
Moreover, a film that does not cause curling or blocking has not yet been obtained. On the other hand, a method has also been proposed in which a solid filler is added to the resin side, which has a higher molding shrinkage rate, in a laminated film, but although this method is effective in preventing curling, it has the disadvantage that it cannot satisfy the requirements for transparency. There is.

本発明は上記従来の欠点を防止して、透明性にすぐれる
とともにカールやブロッキングのない筒状積層フィルム
を提供することを特徴とする特許である。
The present invention is a patent that is characterized by preventing the above-mentioned conventional drawbacks and providing a cylindrical laminated film that has excellent transparency and is free from curling and blocking.

すなわち本発明は、少なくとも二層の結晶性熱可塑性樹
脂層からなる筒状積層フィルムを製造するにあたり、内
層の結晶性熱可塑性樹脂として外層の結晶性熱可塑性樹
脂よりも相対的に融点が高い樹脂を用い、下吹き水冷イ
ンフレーション成形することを特徴とする筒状秋層フィ
ルムの製造方法を提供するものである。
That is, in producing a cylindrical laminated film consisting of at least two crystalline thermoplastic resin layers, the present invention uses a resin having a relatively higher melting point as the inner layer crystalline thermoplastic resin than the outer layer crystalline thermoplastic resin. The present invention provides a method for producing a cylindrical fall layer film, which is characterized by bottom-blown water-cooled inflation molding.

本発明において用いる結晶性熱可塑性樹脂としては特に
制限はなく、様々なものが挙げられる。
The crystalline thermoplastic resin used in the present invention is not particularly limited, and various resins may be used.

例えば高密度ポリエチレン、中密度ポリエチレン。For example, high density polyethylene, medium density polyethylene.

低密度ポリエチレン、エチレンと他のα−オレフィンと
の共重合体、中低工法直鎮状低密度ポリエチレン、ポリ
プロピレン(単独重合体、他のα−オレフィンとの共重
合体、ランダム共重合体)。
Low-density polyethylene, copolymers of ethylene and other α-olefins, low-density low-density polyethylene with medium-low construction method, polypropylene (homopolymers, copolymers with other α-olefins, random copolymers).

ポリブテン−1,ポリ4−メチルペンテン−1などのポ
リオレンイン;ナイロン 6.ナイロン66などのポリ
アミド;ポリエステル等を挙げることができる。
Polyolefins such as polybutene-1 and poly4-methylpentene-1; nylon 6. Examples include polyamides such as nylon 66; polyesters.

本発明は上記結晶性熱可塑性樹脂を用い、少なくども内
外二層からなる筒状積層フィルムを製造するものである
が、ここで内・外層として用いる結晶性熱可塑性樹脂は
特定の関係にあるものを使用することが必要である。
The present invention uses the above-mentioned crystalline thermoplastic resin to produce a cylindrical laminated film consisting of at least two layers, the inner and outer layers, and the crystalline thermoplastic resins used as the inner and outer layers have a specific relationship. It is necessary to use

すなわち、内層の結晶性熱可塑性樹脂として外層の結晶
性熱可塑性樹脂よりも相対的に融点が高い宿脂を用いる
That is, as the crystalline thermoplastic resin for the inner layer, a resin whose melting point is relatively higher than that of the crystalline thermoplastic resin for the outer layer is used.

内層の結晶性熱可塑性樹脂は外層の結晶性熱可塑性樹脂
との関係において、相対的により融点が高いものな用い
ればよいのであって、用いる外層フィルムの融点に基い
て適宜選択される。
The crystalline thermoplastic resin for the inner layer may have a relatively higher melting point in relation to the crystalline thermoplastic resin for the outer layer, and is appropriately selected based on the melting point of the outer layer film used.

以下に上記例示した結晶性熱可塑性樹脂の融点を示す。The melting points of the crystalline thermoplastic resins exemplified above are shown below.

高密度ポリエチレンの融点は通常125〜135°C1
低密度ポリエチレンの融点は通常110〜130°C1
ポリプロピレンの融点は通常160〜180”C,ナイ
ロン6の融点は通常225°C1ナイロン66の融点は
通常265℃、ポリエチレンテレフタレートの融点は適
格265°Cである。
The melting point of high-density polyethylene is usually 125-135°C1
The melting point of low density polyethylene is usually 110-130°C1
The melting point of polypropylene is typically 160-180''C, the melting point of nylon 6 is typically 225°C, the melting point of nylon 66 is typically 265°C, and the melting point of polyethylene terephthalate is typically 265°C.

また、内層の結晶性熱可塑性樹脂の融点は外層の結晶性
熱可塑性樹脂の融点よりも相対的に高いものを用いれば
よいが、好ましくは5℃以上高いもの、より好ましくは
lO°C以上高いものを用いる。これは外層の結晶性熱
可塑性樹脂を急冷結晶化固定する温度条件では内層の温
度は外層に比べ10〜50℃程度高くなっているからで
ある。
Further, the melting point of the crystalline thermoplastic resin for the inner layer may be relatively higher than that of the crystalline thermoplastic resin for the outer layer, but it is preferably 5°C or more higher, more preferably 10°C or more higher. use something This is because under the temperature conditions for rapidly cooling and crystallizing the crystalline thermoplastic resin in the outer layer, the temperature of the inner layer is about 10 to 50° C. higher than that of the outer layer.

さらに上記内層と外層の層厚比は外層:内層=30 :
 70〜97:3の範囲で適宜選択すればよい。ここで
全層に対する内層の比が3%以下ではフィルムの成形性
が困難になると共に、カールを防止するという本発明方
法の効果が十分達成されない。
Furthermore, the layer thickness ratio between the inner layer and the outer layer is outer layer:inner layer=30:
It may be appropriately selected within the range of 70 to 97:3. If the ratio of the inner layer to the total layer is less than 3%, the formability of the film becomes difficult and the effect of the method of the present invention of preventing curling is not sufficiently achieved.

なお、内層の結晶性熱可塑性樹脂には必要により結晶核
剤を添加し融点を高めたり結晶化速度を早めたりするこ
ともできる。この結晶核剤の添加により結晶性熱可塑性
樹脂の結晶核生成速度を規制し、結晶化速度を早めると
同時に、結晶の大きさを抑制することができる。このよ
うな結晶核剤には、有機系核剤として、有機酸の金属塩
、例えハ安息香酸、シクロヘキサンカルボン酸、ジフェ
ニル酢酸、イソニコチン酸、アジピン酸、七ノ(シン酸
、フタル酸、ベンゼンスルホン酸、yvコール酸等のマ
グネシウム、カルシウム、ナトリウム。
In addition, if necessary, a crystal nucleating agent may be added to the crystalline thermoplastic resin of the inner layer to increase the melting point or speed up the crystallization rate. By adding this crystal nucleating agent, it is possible to regulate the crystal nucleation rate of the crystalline thermoplastic resin, accelerate the crystallization rate, and at the same time suppress the size of the crystals. Such crystal nucleating agents include organic nucleating agents such as metal salts of organic acids, such as habenzoic acid, cyclohexanecarboxylic acid, diphenylacetic acid, isonicotinic acid, adipic acid, heptano(cynic acid, phthalic acid, benzene). Magnesium, calcium, sodium such as sulfonic acid, yvcholic acid.

アルミニウム、チタニウムなどの金属塩;有機酸のアミ
ン塩、例えば安、0香酸、フタル酸、アジピン酸等から
誘導されたアミン等がある。無機質の核剤として、シリ
カ、アルミナ、タルク等の微粉末が挙げられる。
Examples include metal salts such as aluminum and titanium; amine salts of organic acids, such as amines derived from ammonium, fragrant acid, phthalic acid, adipic acid, and the like. Examples of the inorganic nucleating agent include fine powders of silica, alumina, talc, and the like.

また、上記内・外層の中間に中間層として他の結晶性熱
可塑性樹脂を用いてもよい。
Further, another crystalline thermoplastic resin may be used as an intermediate layer between the inner and outer layers.

さらに、各結晶性熱可塑性病脂層には安定剤(ra化防
止剤、熱分解防止剤など)、アンチブロッキング剤、ス
リップ剤2着色剤、充填剤等の各腫添加剤を本発明の目
的を損わない範囲で添加することもできる。
Furthermore, each crystalline thermoplastic disease layer contains various additives such as stabilizers (RA prevention agents, thermal decomposition inhibitors, etc.), anti-blocking agents, slip agents, colorants, fillers, etc. for the purpose of the present invention. It can also be added within a range that does not impair it.

本発明は内・外層に上記の如く特定の関係を有する結晶
性熱可塑性樹脂を用い、これを下吹き水冷インフレーシ
ョン成形することを特徴とするものである。
The present invention is characterized in that a crystalline thermoplastic resin having a specific relationship as described above is used for the inner and outer layers, and is subjected to bottom-blown water-cooled inflation molding.

すなわち、まず内層および外層として用〜・る上記の結
晶性熱可塑性樹脂および必要により用いる各種添加剤を
既知の押出成形機に供給し、溶融混練した後、サーキュ
ラ−・ダイに導入する。次いでこれを下向きに押出し、
下吹き水冷インフレーション成形により急冷する。第1
図は下吹きインフレーション成形の1例を示す説明図で
ある。ここでは冷却水を直接バブルに接触させる方法を
示したが、冷却水を霧状にして接融させる方法を採用す
ることもできる。図中、符号1は押出成形機。
That is, first, the above crystalline thermoplastic resin used as the inner layer and the outer layer and various additives used as necessary are supplied to a known extrusion molding machine, melted and kneaded, and then introduced into a circular die. Then push it downwards,
Rapidly cool by bottom-blown water-cooled inflation molding. 1st
The figure is an explanatory diagram showing an example of bottom-blown inflation molding. Although a method of bringing the cooling water into direct contact with the bubbles has been shown here, a method of making the cooling water into a mist and melting it may also be adopted. In the figure, numeral 1 is an extrusion molding machine.

2はサーキュラ−・ダイ、3はエヤーリング、4は冷却
水、5は積層フィルムである。なお、冷却水の温度は通
常10〜40”C1好ましくは15〜35℃である。ま
た、ブローアツプ比は通常0.8〜3、好ましくは1.
1〜2.5である。
2 is a circular die, 3 is an air ring, 4 is a cooling water, and 5 is a laminated film. The temperature of the cooling water is usually 10 to 40"C, preferably 15 to 35C. The blowup ratio is usually 0.8 to 3, preferably 1.
It is 1 to 2.5.

なお、本発明の方法においては上記した冷却速度、使用
する結晶性熱可塑性樹脂1層厚比などを考慮して最適条
件を決定すればよい。
In addition, in the method of the present invention, the optimum conditions may be determined by considering the above-mentioned cooling rate, the thickness ratio of one layer of the crystalline thermoplastic resin used, and the like.

本発明の方法では上記した如く、内・外層に特定の関係
を有する結晶性熱可塑性樹脂を用い、これを下吹き水冷
インフレーション成形により急冷しているので、カール
が全くなく、しかも透明性にすぐれたフィルムを得るこ
とができる。カールの発生が防止できる理由については
明らかでない点もあるが、次のように考えられる。すな
わち、カールは外層の結晶性熱可塑性樹脂が急冷結晶化
固定した後、内層の結晶性熱可塑性樹脂が遅れて結晶化
するため発生すると考えられているが、本発明の方法に
よれば外層の結晶性熱可塑性樹脂が急冷結晶化固定する
温度条件において、その時の内層の温度で結晶化する結
晶性熱可塑性樹脂をこの内層として用いているので、内
・外層がほぼ同時に結晶化固定化するからである。
As mentioned above, in the method of the present invention, a crystalline thermoplastic resin having a specific relationship is used for the inner and outer layers, and this is rapidly cooled by bottom-blown water-cooled inflation molding, so there is no curling at all and it has excellent transparency. It is possible to obtain a film that is The reason why curling can be prevented is not clear, but it is thought to be as follows. That is, it is believed that curling occurs because the crystalline thermoplastic resin in the inner layer crystallizes after the crystalline thermoplastic resin in the outer layer is rapidly cooled and crystallized, but according to the method of the present invention, curling occurs in the outer layer. Under the temperature conditions where the crystalline thermoplastic resin is rapidly crystallized and fixed, the inner layer is made of a crystalline thermoplastic resin that crystallizes at the temperature of the inner layer at that time, so the inner and outer layers are crystallized and fixed almost simultaneously. It is.

さらに本発す」の方法によれば、ブロッキングがなく開
口性にすぐれたフィルムを得ることができ、しかモアン
チブロツキング剤などの添加量が少なくてよい。また、
本発明の方法は従来の方法よりもフィルムを急冷するこ
とができるため生産性にもすぐれたものである。
Furthermore, according to the method of the present invention, a film with no blocking and excellent opening properties can be obtained, and only a small amount of anti-blocking agent and the like can be added. Also,
The method of the present invention has superior productivity because it can cool the film more rapidly than conventional methods.

したがって、本発明の方法は各種包装に用いる筒状積層
フィルムの製造に有効に利用することができる。
Therefore, the method of the present invention can be effectively used for manufacturing cylindrical laminated films used for various types of packaging.

次に本発明を実施例により説明する。Next, the present invention will be explained by examples.

実施例 50mmφ、Lカー26の2台の押出機を用い、外層用
結晶性熱可塑性樹脂としてエチレン−オクテン−1共重
合体(密度0.927 g/crrt3.メルトインデ
ックス(MI ) 4.99710分、融点125℃)
、内層用結晶性熱可塑性樹脂としてポリプロピレン(密
度o、91g/aが、MI 79/1o分、融点170
°C)を押出成形機に供給し溶融混練した後、ダイ内接
着型サーキュラ−・ダイ(150mrptφ、ダイリッ
プ間隙2mm)に導入し、次いで下向きに押出し、ブロ
ーアツプ比1.3で下吹き水冷インフレーション成形を
行ない厚み40μ(外層:内層=872)の共押出積層
二層フィルムを製造した。
Example Using two extruders with a diameter of 50 mm and an L car of 26, ethylene-octene-1 copolymer (density 0.927 g/crrt3. Melt index (MI) 4.99710 minutes) was used as the crystalline thermoplastic resin for the outer layer. , melting point 125℃)
, polypropylene (density o, 91 g/a, MI 79/1o min, melting point 170) was used as the crystalline thermoplastic resin for the inner layer.
°C) was fed into an extruder and melted and kneaded, then introduced into an in-die adhesive circular die (150 mrptφ, die lip gap 2 mm), extruded downward, and subjected to bottom-blown water-cooled inflation molding at a blow-up ratio of 1.3. A coextrusion laminated two-layer film having a thickness of 40 μm (outer layer: inner layer = 872) was produced by carrying out the following steps.

得られたフィルムはカールがまったくなく、霞度2.1
%、光沢152%であって開口性にすぐれたものであっ
た。
The obtained film had no curl at all and had a haze level of 2.1.
%, gloss of 152%, and excellent opening properties.

比較例 実施例において、外層用結晶性熱可塑性樹脂として用い
たエチレン−オクテン−1共重合体のみを使用したこと
以外は実施例に準じて行ない厚み40μの単層フィルム
を得た。
Comparative Example A monolayer film having a thickness of 40 μm was obtained in the same manner as in the Example except that only the ethylene-octene-1 copolymer used as the crystalline thermoplastic resin for the outer layer was used.

得られたフィルムはまったく開口性が悪く、しかも開口
した7・イルムは内側に激しくカールしておりフィルム
としての使用にはまったく適さないものであった。
The resulting film had poor opening properties, and moreover, the opened 7-ilms were severely curled inward, making them completely unsuitable for use as a film.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は下吹きインフレーション成形の1例を示す説明
図である。 l・・・押出成形機、2・・・サーキュラ−・ダイ。 3・・・エヤーリング、4・・・冷却水、5・・・積層
フィ特許出願人 出光石油化学株式会社
FIG. 1 is an explanatory diagram showing an example of bottom-blown inflation molding. l...Extrusion molding machine, 2...Circular die. 3...Air ring, 4...Cooling water, 5...Laminated film Patent applicant Idemitsu Petrochemical Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 1、少なくとも二層の結晶性熱可塑性樹脂層からなる筒
状積層フィルムを製造するにあたり、内層の結晶性熱可
塑性樹脂として外層の結晶性熱可塑性樹脂よりも相対的
に融点が高い樹脂を用い、下吹き水冷インフレーション
成形することを特徴とする筒状積層フィルムの製造方法
1. In producing a cylindrical laminated film consisting of at least two crystalline thermoplastic resin layers, a resin having a relatively higher melting point than the crystalline thermoplastic resin of the outer layer is used as the crystalline thermoplastic resin of the inner layer, A method for producing a cylindrical laminated film characterized by bottom-blown water-cooled inflation molding.
JP58114308A 1983-06-27 1983-06-27 Manufacture of cylindrical laminated film Granted JPS606431A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58114308A JPS606431A (en) 1983-06-27 1983-06-27 Manufacture of cylindrical laminated film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58114308A JPS606431A (en) 1983-06-27 1983-06-27 Manufacture of cylindrical laminated film

Publications (2)

Publication Number Publication Date
JPS606431A true JPS606431A (en) 1985-01-14
JPH0261376B2 JPH0261376B2 (en) 1990-12-19

Family

ID=14634615

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58114308A Granted JPS606431A (en) 1983-06-27 1983-06-27 Manufacture of cylindrical laminated film

Country Status (1)

Country Link
JP (1) JPS606431A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1987003533A1 (en) * 1985-12-16 1987-06-18 Exxon Chemical Patents, Inc. Method for making composite films
JPH0647538U (en) * 1992-10-12 1994-06-28 立山アルミニウム工業株式会社 Door handle
CN102615758A (en) * 2012-04-05 2012-08-01 北京化工大学 Combined laminated composite calendering production line for multi-layer rubber sheet and compounding method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57176123A (en) * 1981-04-23 1982-10-29 Ube Nitto Kasei Kk Method and apparatus for manufacturing interlaminar hollow film

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57176123A (en) * 1981-04-23 1982-10-29 Ube Nitto Kasei Kk Method and apparatus for manufacturing interlaminar hollow film

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1987003533A1 (en) * 1985-12-16 1987-06-18 Exxon Chemical Patents, Inc. Method for making composite films
JPH0647538U (en) * 1992-10-12 1994-06-28 立山アルミニウム工業株式会社 Door handle
CN102615758A (en) * 2012-04-05 2012-08-01 北京化工大学 Combined laminated composite calendering production line for multi-layer rubber sheet and compounding method
CN102615758B (en) * 2012-04-05 2014-04-16 北京化工大学 Combined laminated composite calendering production line for multi-layer rubber sheet and compounding method

Also Published As

Publication number Publication date
JPH0261376B2 (en) 1990-12-19

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