JPS61108549A - Laminate - Google Patents

Laminate

Info

Publication number
JPS61108549A
JPS61108549A JP59229660A JP22966084A JPS61108549A JP S61108549 A JPS61108549 A JP S61108549A JP 59229660 A JP59229660 A JP 59229660A JP 22966084 A JP22966084 A JP 22966084A JP S61108549 A JPS61108549 A JP S61108549A
Authority
JP
Japan
Prior art keywords
ldpe
layer
laminate
paper
odor
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
JP59229660A
Other languages
Japanese (ja)
Other versions
JPH0463776B2 (en
Inventor
石崎 美弘
明博 松本
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.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi 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 Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP59229660A priority Critical patent/JPS61108549A/en
Publication of JPS61108549A publication Critical patent/JPS61108549A/en
Publication of JPH0463776B2 publication Critical patent/JPH0463776B2/ja
Granted legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、基材や接着剤の臭いや味が包装内容物中へ拡
散するのを防ぐ積層体に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a laminate that prevents odors and tastes from base materials and adhesives from diffusing into package contents.

(従来の技術) 近年、ポリオレフィン系樹脂(以下POと略記する)は
、セロハン、ポリエチレンテレフタレート(以下PET
と略記する)、紙あるいはアルミニウム(以下Mと略記
する)等とラミネーションして食品包装あるいけ医薬品
包材等に用いられている。
(Prior art) In recent years, polyolefin resins (hereinafter abbreviated as PO) have been widely used, such as cellophane, polyethylene terephthalate (hereinafter PET), etc.
It is laminated with paper, aluminum (hereinafter abbreviated as M), etc., and used for food packaging, pharmaceutical packaging, etc.

例えば、PET等の基材にアンカーコート等の前処理を
した上に低密度ポリエチレン(以下LDPEと略記する
)を高温(320℃)で押出して積層させる押出コーテ
ィング方法、PET等の基材に、コロナ処理等で前処理
したLDPEフィルムまたはシートを接着剤を介して積
層するドライラミネート方法、または、LDPEを高温
(320℃)および低温(280℃)で共押出し成形し
たものをPET等の基材に積層させる方法が為されてい
る。
For example, an extrusion coating method in which a base material such as PET is pretreated with an anchor coat, etc., and then low density polyethylene (hereinafter abbreviated as LDPE) is extruded and laminated at high temperature (320°C), Dry lamination method in which LDPE films or sheets pretreated with corona treatment etc. are laminated via adhesive, or LDPE is co-extruded at high temperature (320°C) and low temperature (280°C) and used as a base material such as PET. A method has been used in which layers are stacked on top of each other.

(発明が解決しようとする問題点) しかしながら、押出コーティングの場合はLDPKが非
常に高温で押出されるので、LDPEの分解物の臭いや
味が内容物中に移行する。また、ドライラミネーション
の場合け、コロナ処理に起因する臭い、あるいは、接着
剤または有機溶剤の臭いや味がLDPEを透過して内容
物中に移行する。さらに共押出し成形の場合は、高温(
320℃)押出しによる分解物の臭いや味が低温(28
0℃)押出物を透過して内容物中に移行する、これらの
ように内容物の臭いや味は、ものによっては商品価値を
落とす欠点となる。
(Problems to be Solved by the Invention) However, in the case of extrusion coating, LDPK is extruded at a very high temperature, so the odor and taste of decomposed LDPE products migrate into the contents. In addition, in the case of dry lamination, the odor caused by the corona treatment or the odor or taste of the adhesive or organic solvent passes through the LDPE and migrates into the contents. Furthermore, in the case of coextrusion molding, high temperatures (
320℃) The odor and taste of the decomposed products from extrusion are reduced at low temperatures (28℃).
(0°C) The odor and taste of the contents, which pass through the extrudate and migrate into the contents, can be a drawback that lowers the commercial value depending on the product.

特に最近、ミネラルウォーター、酒、果汁等の包装にお
いて、臭いや味の移行の少ない包装体の使用が望まれて
いる。これらは、少しでも包装体の臭いが移行すると著
しぐ商品価値を落とすので、その改善の要求が大きい。
Particularly recently, in the packaging of mineral water, alcoholic beverages, fruit juices, etc., there has been a desire to use packaging materials with less transfer of odor and taste. If even a small amount of odor is transferred to these products, the commercial value of these products will be significantly reduced, so there is a great demand for improvement.

(問題を解決するための手段) 本発明け、かかる要求を満たすことを目的と1−1特定
のガスバリヤ一層を設けて、ある条件で成形することに
より、この目的が達成されることを見イ出1.て為慣れ
たものである。
(Means for Solving the Problem) The present invention aims to meet such requirements by providing a specific gas barrier layer and molding under certain conditions. Out 1. I'm used to it.

即ち、本発明は、「23℃乾燥下での酸素透過)   
     ガ゛゛°“/m”−24hr°°“J!TV
)lx′<す“−件樹脂と実質的に無臭のポリオレフィ
ン系樹脂を140〜290℃で共押出し成形し、次いで
該ガスバリヤー性樹脂層を基材と積層させた稍層物にお
いで、該ガスバリヤー性樹脂層の厚みが1〜30μで該
ポリオレフィン系樹脂層が10〜200μであることを
特徴とする積層体」である。
That is, the present invention provides "oxygen permeation under dry conditions at 23°C".
GA゛゛°“/m”-24hr°°“J!TV
) lx'<s "- The resin and the substantially odorless polyolefin resin are coextruded at 140 to 290°C, and then the gas barrier resin layer is laminated with the base material to form a thin layered product. A laminate characterized in that the gas barrier resin layer has a thickness of 1 to 30μ and the polyolefin resin layer has a thickness of 10 to 200μ.

(作用) 本発明で用いるガスバリヤ−性樹脂は、23℃乾燥下で
の酸素透過度が5occ/−・24 hr・atm以下
、好ましくは1 occ/i −24hr−atm以下
、特に好ましくけ5 CC/FF/ −24hr−at
m以下のもので、例えば、エチレン−酢酸ビニル共重合
体のケン化物(以下IV、OHと略記する)、ポリビニ
ルアルコール、ポリアクリロニトリル系樹脂、ポリ塩化
ビニリデン等が好ましい。
(Function) The gas barrier resin used in the present invention has an oxygen permeability of 5 occ/-24 hr-atm or less, preferably 1 occ/i-24 hr-atm or less, particularly preferably 5 CC when dried at 23°C. /FF/ -24hr-at
m or less, for example, saponified ethylene-vinyl acetate copolymers (hereinafter abbreviated as IV and OH), polyvinyl alcohol, polyacrylonitrile resins, polyvinylidene chloride, etc. are preferable.

酸素透過度が上記以外のものは、本発明の効果が低く実
用性に欠ける。
If the oxygen permeability is other than the above, the effect of the present invention is low and it lacks practicality.

また、本発明で用いる実質的に無臭のPOとしては、具
体的には例えば、LDPE、高密度ポリエチレン(以下
I(D PEと略記する)、ポリプロピレン(以下PP
と略記する)、エチレン−プロピレン共重合体、エチレ
ン−α−オレフィン直鎖状共重合体、エチレン−アクリ
ル酸共重合体(以下EAAと略記する)、エチレン−酢
酸ビニル共重合体(以下EVAと略記する)等を挙げる
ことができる。
In addition, the substantially odorless PO used in the present invention is specifically, for example, LDPE, high density polyethylene (hereinafter abbreviated as DPE), polypropylene (hereinafter PP), etc.
), ethylene-propylene copolymer, ethylene-α-olefin linear copolymer, ethylene-acrylic acid copolymer (hereinafter abbreviated as EAA), ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVA), (abbreviated)).

ここで、実質的に無臭とけ、臭いをかいでみて殆んど臭
いを感じないことを言うが、評価法としに てけ、次の官能試験法(以下〆法と略記する)において
に失点が1未満であるものが実用的であり、実質的に無
臭と言える。
Here, I am referring to the fact that it melts virtually odorless, and when I smell it, I don't notice any odor, but as an evaluation method, the following sensory test method (hereinafter abbreviated as "method") loses 1 point. It is practical to have less than 100% odor, and it can be said that it is substantially odorless.

つまり、ペレット4Ofを5001117の栓付きフラ
スコに採取して栓をした後、40tlCで1−間加熱す
る。次に室温寸で冷却した後、東京都公害研究所提案の
ランク(O・・・無臭、1・・・弱く臭う、2・・・は
っきり臭う、3・・・強く臭く)に従って評点し、7人
のパネラ−のイ均点数(以下に失点と略記する)をデー
ターとした。
That is, the pellets 4Of are collected in a stoppered flask 5001117 and the flask is stoppered, and then heated at 40 tlC for 1 hour. Next, after cooling to room temperature, it was rated according to the ranking proposed by the Tokyo Metropolitan Pollution Research Institute (O: no odor, 1: weak odor, 2: distinct odor, 3: strong odor). The average score (hereinafter abbreviated as points conceded) of the human panelists was used as data.

本発明に〉いては、ガスバリヤ−性樹脂と実質的に無臭
のPOとi’t140〜290℃、好ましくけ140〜
260.特に好ましくは140〜200℃で共押出し成
形して二層積層体(以下BS層と略記する)を製造する
が、140℃未満では樹脂の延展性が不足して成膜性能
がなくなり、一方、290℃超過では折角の無臭POに
臭いや味がつぐようになる。
In the present invention, the gas barrier resin and substantially odorless PO are combined at 140 to 290°C, preferably at 140 to 290°C.
260. Particularly preferably, a two-layer laminate (hereinafter abbreviated as BS layer) is produced by coextrusion molding at a temperature of 140 to 200°C; however, below 140°C, the ductility of the resin is insufficient and film forming performance is lost; If the temperature exceeds 290°C, the odor and taste will overwhelm the odorless PO.

このとき、ガスバリヤ−性樹脂の厚みは1〜30p1好
ましくけ10〜20μ、また、無臭poの厚みは10〜
200μ、好ましくFii s〜100戸で成形する。
At this time, the thickness of the gas barrier resin is 1 to 30μ, preferably 10 to 20μ, and the thickness of the odorless po is 10 to 30μ.
200μ, preferably Fii s~100 units.

ガスバリヤ−性樹脂の厚みが1μ未満では防臭が達成さ
れず、一方、30μ超過では包装材料としての経済性を
欠ぐ。また、無臭POの厚みが10p未満ではヒートシ
ール強度が不足し、一方、200μ超過では経済性を欠
くので好ましくない。
If the thickness of the gas barrier resin is less than 1 μm, odor control will not be achieved, while if it exceeds 30 μm, it will be uneconomical as a packaging material. Moreover, if the thickness of the odorless PO is less than 10 μm, the heat sealing strength will be insufficient, while if it exceeds 200 μm, it will be unfavorable because it will lack economic efficiency.

斯様にして得られたBS層は、次いで該ガスバリヤー性
樹脂層が基材と積層される。基材としては、セロハン、
PET、ナイロンあるいはOPP等の樹脂、Mのような
金属、紙、布およびPI/M%PE/紙あるいはPK/
紙/ P E / At等の積面と略記する)と基材と
を貼りあわせる方法は、両面をそのまま共押出しする方
法、または盛装に応じて公知の接着剤、例えば、ポリウ
レタンやイソシアネート系等の接着剤を用いてドライラ
ミネートする方法、あるいはLDPEやFAA等の軟る
方法等がある。
The BS layer thus obtained is then laminated with the gas barrier resin layer on a base material. The base material is cellophane,
Resin such as PET, nylon or OPP, metal such as M, paper, cloth and PI/M%PE/paper or PK/
The method for bonding paper/PE/At, etc.) and the base material is to co-extrude both sides as they are, or to use a known adhesive such as polyurethane or isocyanate based adhesive depending on the packaging. There are methods such as dry lamination using an adhesive, and methods using soft materials such as LDPE and FAA.

このとき、B層面や基材面を公知の表面処理(プライマ
ー処理、コロナ処理、プラズマ処理等)を施こしたり、
B層内に押出可能な実質的無臭の接着性樹脂、例えば、
無水マレイン酸変性ポリオレフィン等を予め含有させて
おいなり、ま7’l:は、B層面若しくは基材面に予め
変性ポリオレフィンのような接着性樹脂を共押出し接着
しておき、貼合わせに資することは、接着性や貼り合わ
せ加工性の向上に役立つ。
At this time, the B layer surface and the base material surface are subjected to known surface treatments (primer treatment, corona treatment, plasma treatment, etc.),
A substantially odorless adhesive resin extrudable into layer B, e.g.
Pre-containing maleic anhydride-modified polyolefin or the like, or coextruding an adhesive resin such as modified polyolefin onto the B layer surface or base material surface in advance to facilitate lamination. is useful for improving adhesion and lamination processability.

1       (実施例) 実施例1 メルトフローレー) 4.4 f710分、密度1.1
9t/aS工チレン含量32モルチのエチレン−酢酸ビ
ニル共電合体(EVOH)とメルトフローレ−) 8 
f/10分、密度0.91 s t/cr1%に失点0
.3の低密度ポリエチレン(LDPE)を口径65醜の
2台の押出機を設けた共押出しインフレータ ゛ヨン成
形機にて、EVOHの樹Pl温度を215℃、LDPE
の樹脂温度を180℃とし、引き取り速度を30m/分
で共押出し成形し、EVOH層が15μ、LDPE層が
30μ、合計45μの88層フィルムを作成した。
1 (Example) Example 1 Melt Flow Ray) 4.4 f710 min, density 1.1
Ethylene-vinyl acetate coelectrolyte (EVOH) with a 9t/aS ethylene content of 32 molt and melt flow rate) 8
f/10 min, density 0.91 s t/cr 1% and 0 points
.. Using a co-extrusion inflator molding machine equipped with two extruders with a diameter of 65 mm, low-density polyethylene (LDPE) was heated to 215 degrees Celsius, and the LDPE was heated to 215 degrees Celsius.
Coextrusion molding was carried out at a resin temperature of 180° C. and a take-off speed of 30 m/min to create an 88-layer film with an EVOH layer of 15 μm, an LDPE layer of 30 μm, and a total thickness of 45 μm.

一方、口径9(1mの押出機に装着したTダイから、先
と同じLDPEを樹脂温度320℃で押出して溶融フィ
ルムとなし、これをコロナ放電表面処理(30W−分/
FF!’) L7’!:2 o o t/−のカートン
紙と圧着ロールで圧着してラミネートシ、LDPE/カ
ートン紙の積層基材とした。
On the other hand, the same LDPE as before was extruded at a resin temperature of 320°C through a T-die attached to an extruder with a diameter of 9 (1 m) to form a molten film, which was then subjected to corona discharge surface treatment (30 W-min/min).
FF! ') L7'! :2 o o t/- carton paper was pressed with a pressure roll to obtain a laminated sheet, a laminated base material of LDPE/carton paper.

ここでLDPE層aisμとした。Here, the LDPE layer was defined as aisμ.

次に、先の88層フィルムのEVOH層(B/43面に
イソシアネート系アンカーコート剤(AC)溶液を塗布
後に溶剤を乾燥させてプライマーコートしたBS層を用
意した。次いで、口径90−の押出機に装着したTダイ
から、先と同じLDPKを樹脂温度320℃で押出して
溶融フィルムとなし、これを先のプライマーコートした
BS層のB層面とLDpEii−)ン紙層の紙面との間
に接着剤としてはさみ圧着ロールで圧着してサンドイッ
チラミネートした。このラミネート速度は8゜m7分、
接着層であるLDPE層は厚み15μとした。
Next, a BS layer was prepared by coating the EVOH layer (B/43 side) of the previous 88-layer film with an isocyanate anchor coating agent (AC) solution and then drying the solvent and coating with a primer. From the T-die attached to the machine, extrude the same LDPK as before at a resin temperature of 320°C to form a molten film, and place this between the B layer surface of the BS layer coated with the primer and the paper surface of the LDpEii-)n paper layer. Sandwich lamination was performed by pressing with a scissor pressure roll as an adhesive. This lamination speed is 8゜7 minutes,
The LDPE layer serving as the adhesive layer had a thickness of 15 μm.

得られた積層体の構成は、最外層側から、LDPE(1
5μm320℃)/紙/LDPE (15μm320℃
) /AC/EVOH(1s p −215’C)/L
DPE (30μm180℃)である。
The structure of the obtained laminate was as follows: LDPE (1
5μm 320℃)/Paper/LDPE (15μm 320℃
) /AC/EVOH(1s p -215'C)/L
DPE (30 μm, 180° C.).

実施例2 実施例1における2層からなる88層フィルムと に代えて、先β同じEVOH,メルトフローレー)1.
3F/10分、密度0.90 ? /cl!!、マレイ
ン酸含量0.1重量%、K法点0.3の無水マレイン酸
変性低密度ポリエチレンおよび先と同じLDPEを口径
65咽の3台の押出機を設けた共押出しインフレーショ
ン成形機にてEVOHを21m℃、変性ポリエチレンを
215℃およびLDPKを180℃で実施例1と同様に
して3層成形し、EVOH15μ、変性ポリエチレン1
5μおよびLDPE30μで合計60μの88層フィル
ムを作成し、これを用いた外は実施例1と同様の方法で
、最外層側から、LDPE(15μ)/紙/I、DPE
(tsμ)/AC/EVOH(xsμ)/変性ポリエチ
レン(15μ)/LDPK(30μ)の構成の積層体を
作成した。
Example 2 In place of the 88-layer film consisting of two layers in Example 1, the same EVOH (EVOH, melt flow) 1.
3F/10 minutes, density 0.90? /cl! ! , maleic anhydride-modified low-density polyethylene with a maleic acid content of 0.1% by weight and a K point of 0.3, and the same LDPE as above were processed into EVOH using a coextrusion inflation molding machine equipped with three extruders each having a diameter of 65 mm. Three layers were molded in the same manner as in Example 1 at 21m℃, modified polyethylene at 215℃, and LDPK at 180℃, EVOH 15μ, modified polyethylene 1
An 88-layer film with a total of 60μ was prepared using 5μ and 30μ of LDPE, and in the same manner as in Example 1, starting from the outermost layer, LDPE (15μ)/paper/I, DPE
A laminate having a configuration of (tsμ)/AC/EVOH (xsμ)/modified polyethylene (15μ)/LDPK (30μ) was prepared.

実施例3 実施例2におけるEVOH層の厚みを2μとした外は実
施例2と同様の方法で、最外層側から、LDPE(15
μ)/紙/LDPE (15μ)/AC/EVOH(2
/j)/変性ポ1.lzチレ:/(15μ)/LDPE
 (30μ)の構成の積層体を作成した。
Example 3 In the same manner as in Example 2 except that the thickness of the EVOH layer in Example 2 was changed to 2 μm, LDPE (15 μm) was added from the outermost layer side.
μ)/Paper/LDPE (15μ)/AC/EVOH (2
/j)/denatured po1. lzChile: /(15μ)/LDPE
A laminate having a configuration of (30μ) was created.

実施例4 実施例2におけるEVOH層の厚みを1μとした外は実
施例2と同様の方法で、最外層側から、LDPE (1
5μ)/紙/LDPK(15μ)/AC/EVOH(1
μ)/変性ポリエチレン(15μ)/LDPE (30
μ゛)の構成の積層体を作成した。
Example 4 Using the same method as in Example 2 except that the thickness of the EVOH layer in Example 2 was changed to 1 μm, LDPE (1 μm
5μ)/Paper/LDPK(15μ)/AC/EVOH(1
μ)/modified polyethylene (15μ)/LDPE (30
A laminate having the configuration μ゛) was created.

実施例5 実施例2における88層フィルムのLDPEに代tて、
メルトフローレート9 y/x o分、密度0.944
 ylcds K失点0.2の高密度ポリエチレン(H
DPK)を用い、さらに最外層のI、DPEに代えて同
上のHDPIを、用いた外は実施例2と同様の方法で、
最外層から、HDPE(15,#)/紙/LDPE (
15P 1 /AC/EVOH(15p)/変性ポリエ
チレン(15μ)/HDPE(30μ)の構成の積層体
を作成した。
Example 5 Instead of LDPE in the 88-layer film in Example 2,
Melt flow rate 9 y/x o min, density 0.944
ylcds High-density polyethylene (H
DPK), and in the same manner as in Example 2, except that the same HDPI as above was used in place of I and DPE in the outermost layer,
From the outermost layer, HDPE (15, #)/Paper/LDPE (
A laminate having a composition of 15P 1 /AC/EVOH (15p)/modified polyethylene (15μ)/HDPE (30μ) was created.

実施例6 実施例2と同様の方法で、同様の88層フィルムを作成
した。一方、実施例2と同様の方法で同様のLDPE/
紙なる積層体を作成した。次に、口径90mmの押出機
に装着したTダイから先と同じLDPEを320℃で押
出して溶融フィルムとなし、これを先の積層体の紙面と
厚み7μのMとの間に接着剤としではさみ圧着ロールで
圧着してサンドイッチラミネートし、LDPE (15
μ)/紙/LDPK(15μ)/Atという積層体から
なる基材を作成した。
Example 6 A similar 88-layer film was made in the same manner as in Example 2. On the other hand, similar LDPE/
A paper laminate was created. Next, the same LDPE was extruded at 320°C from a T-die attached to an extruder with a diameter of 90 mm to form a molten film, and this was used as an adhesive between the paper surface of the previous laminate and M with a thickness of 7 μm. Crimp with scissor crimping roll, sandwich laminate, and LDPE (15
A base material consisting of a laminate of μ)/paper/LDPK(15μ)/At was prepared.

一方、iBs層のB層面にイソシアネート系アンカーコ
ート剤でプライマーコートし念。
On the other hand, the B layer surface of the iBs layer was prime coated with an isocyanate anchor coating agent.

次に、口径9(1mの押出機に装着したTダイから、先
と同じLDPKを320℃で押出して溶融フィルムとな
し、これを先のプライマーコートし7tBS層のB層面
と基材のM面との間に接着剤としてId4み圧着ロール
で圧着してサンドインチラミネートした。この時のラミ
ネート速度1d 80 m7分、LDPE層の厚みll
115μとした。得られた積層体の構成は、最外層側か
ら、LDPK(tsμ)/紙/LDPK(1sμ) /
At/LDP E(15P )/AC/EVOH(15
fi )、/変性yN「 リエチレン(15μ)/LDPE(aoμ)である。
Next, the same LDPK as before was extruded at 320°C from a T-die attached to an extruder with a diameter of 9 (1 m) to form a molten film, and this was coated with the primer and applied to the B layer side of the 7tBS layer and the M side of the base material. Sandwich lamination was carried out by pressing Id4 as an adhesive with a pressure roll.The lamination speed at this time was 1d 80 m7 minutes, and the thickness of the LDPE layer was ll.
It was set to 115μ. The structure of the obtained laminate is: LDPK(tsμ)/paper/LDPK(1sμ)/from the outermost layer side.
At/LDP E(15P)/AC/EVOH(15
fi),/modified yN "Liethylene (15μ)/LDPE (aoμ).

実施例7 実施例6と同様の方法で同様のLDPK(15μ)/紙
/LDPE(15μ)/A/という積層体からなる基材
と、EVOH(15μ]/変性ポリエチレン(15μ)
/LDPE (30μ)という構成のBS層を作成した
Example 7 A base material made of the same laminate of LDPK (15μ)/paper/LDPE (15μ)/A/ and EVOH (15μ)/modified polyethylene (15μ) was prepared in the same manner as in Example 6.
A BS layer having a configuration of /LDPE (30μ) was created.

2  次に、BS層のB層面にイソシアネート系アンカ
ーコート剤でプライマーコートし、ポリウレタン系接着
剤を用いてプライマーコー、トシたB層面と基材のM面
とをドライラミネートシ、最外層側から、LDPE(1
5μ)/紙/LDPE(xsμ)/M/接着剤/AC/
EVOH(15μ)/変性ポリエチレン(15μ) /
I、DPE (30μ)の積層体を作成した。
2 Next, apply a primer coat to the B layer side of the BS layer with an isocyanate-based anchor coating agent, apply a primer coat using a polyurethane adhesive, and then dry laminate the B layer side and the M side of the base material, starting from the outermost layer side. ,LDPE(1
5μ)/Paper/LDPE (xsμ)/M/Adhesive/AC/
EVOH (15μ) / modified polyethylene (15μ) /
A laminate of I, DPE (30μ) was prepared.

実施例8 実施例2における88層フィルムを共押出成形する際の
LDPIの樹脂温度を180℃から230℃と1.た外
は実施例2と同様の方法で、最外層側から、LDPE(
15μ)/紙/LDPE (15μ)/AC/EvOH
(15μ)/変性ポリエチレン(15μ)/LDPE(
30μ)の積層体を作成した。
Example 8 The LDPI resin temperature during coextrusion molding of the 88-layer film in Example 2 was varied from 180°C to 230°C. In the same manner as in Example 2, LDPE (
15μ)/Paper/LDPE (15μ)/AC/EvOH
(15μ) / modified polyethylene (15μ) / LDPE (
A laminate with a thickness of 30 μm was prepared.

実施例9 実施例2における88層フィルムに代えて、密度1.1
 a y /a1.キャピラリー粘度計を用いてL/D
=8/2.1各日、剪断速度3,0005ec−”、温
度240℃における見掛は溶融粘度がs、o o 。
Example 9 Instead of the 88 layer film in Example 2, a density of 1.1
ay/a1. L/D using a capillary viscometer
=8/2.1 each day, the shear rate is 3,0005 ec-'', the apparent melt viscosity is s, o o at a temperature of 240°C.

ボイズの6ナイcxノ(以下NYと略記する)を240
℃、変性ポリエチレンを240℃およびLDPKを18
0℃として同様に3層共押出成形し、Ny30μ、変性
ポリエチレン15μおよびLDPK30μで合計75μ
の88層フィルムを得、これを用いた以外は実施例2と
同様にして、最外層側から、LDPE(15μ)/紙/
LDPK (1sμ)/AC/N5F(30μ)/変性
ポリエチレン(15μ)/LDPE (30μ)の積層
体を作成した。
Boy's 6 Nycxno (hereinafter abbreviated as NY) is 240
℃, modified polyethylene at 240℃ and LDPK at 18℃
Three layers were coextruded in the same manner at 0°C, and a total of 75μ was formed using 30μ of Ny, 15μ of modified polyethylene, and 30μ of LDPK.
An 88-layer film of LDPE (15μ)/paper/
A laminate of LDPK (1 sμ)/AC/N5F (30μ)/modified polyethylene (15μ)/LDPE (30μ) was prepared.

比較例1 実施例9におけるNy層の厚みを20μとする外は実施
例9と同様の方法で、最外層から、LDPE(15μ)
/紙/LDPK (15μ)/AC/Ny (20μ)
/変性ポリエチレン(ts、u)/LDPE (30μ
)の積層体を作成した。
Comparative Example 1 LDPE (15μ) was added from the outermost layer in the same manner as in Example 9 except that the thickness of the Ny layer in Example 9 was 20μ.
/Paper/LDPK (15μ)/AC/Ny (20μ)
/ modified polyethylene (ts, u) / LDPE (30μ
) was created.

比較例2 実施例2におけるBS層フィルムのに失点0.3のLD
PEの代わりに、K法点2.5のLDPEを用いた外は
実施例2と同様にして、最外層側から、LDPE(15
μ)/紙/LDPE (1sμ)/AC/EVOH(1
sμ)/変性ポリエチレン(15μ)/LDPE(30
μ、K法点2.5)の積層体を作成した。
Comparative Example 2 LD of BS layer film in Example 2 was 0.3
In the same manner as in Example 2, except that LDPE with a K normal point of 2.5 was used instead of PE, LDPE (15
μ)/Paper/LDPE (1sμ)/AC/EVOH(1
sμ)/modified polyethylene (15μ)/LDPE (30
A laminate with μ and K normal point 2.5) was created.

比較例3 実施例21C:bけるBS層フィルムを共押出成彩する
際のLDPEの樹脂温度を180℃に代えて320℃と
した外は実施例2と同様の方法で、最外層側から、LD
PE(15μ)/紙/LDPE(15μ)/AC,/E
VoH(l s、u)/変性ポリエチレン(15μ)/
LDPE(30μ、320℃)の積層体を作成した。
Comparative Example 3 Example 21C: From the outermost layer side, the same method as Example 2 was used except that the LDPE resin temperature was changed to 320°C instead of 180°C when coextruding the BS layer film. L.D.
PE (15μ)/Paper/LDPE (15μ)/AC, /E
VoH (l s, u)/modified polyethylene (15μ)/
A laminate of LDPE (30μ, 320°C) was prepared.

比較例4 実施例2におけるBS層フィルムのEVOH層を除き、
AC剤コートをしない外は実施例2と同様の方法で、最
外層側から、LDPE(15μ)/紙/LDPE(ls
戸)/変性ポリエチレン(15μ>/LDPE(30μ
)の漕層体を作成した。
Comparative Example 4 Except for the EVOH layer of the BS layer film in Example 2,
In the same manner as in Example 2 except that the AC agent coating was not applied, LDPE (15μ)/paper/LDPE (ls
door)/modified polyethylene (15μ>/LDPE (30μ
) was created.

〈評価〉 以との各側で作成した積層体の臭い、味シよびBS層の
酸素透過量を評価した結果を21表に示す。
<Evaluation> Table 21 shows the results of evaluating the odor and taste of the laminate prepared on each side, as well as the amount of oxygen permeation through the BS layer.

なお、臭めの評価は、各構成の積層体からなる一辺20
ωの四方シールの包を作成してその中へ無臭の空気を2
00CC注入し、40℃で2時間加熱後に1時間放冷し
、容器の一角を切り取り、前述のに法に準じて臭いの官
能試験を行なった。評価は、7人のパネラ−評点の平均
値を取り、その点(0・・・無臭、1・・・弱く臭う、
2・・・はっきり臭う、3・・・仰ぐ臭う)を本って、
0を◎、0〜1を○、1〜2をΔ、2〜3を×で表わし
た。
In addition, odor evaluation was performed on one side of 20 laminates of each configuration.
Create a package with ω seals on all sides and fill it with odorless air 2
00CC was poured into the container, heated at 40° C. for 2 hours, allowed to cool for 1 hour, cut off one corner of the container, and conducted an odor sensory test according to the method described above. The evaluation is based on the average score of the seven panelists, and the score is 0: no odor, 1: weak odor,
2...It smells clearly, 3...It smells great)
0 is represented by ◎, 0 to 1 is represented by ○, 1 to 2 is represented by Δ, and 2 to 3 is represented by ×.

1+、味の評価は、臭いの評価と同じ包を作成・ し、
その中へミネラルウォーター200CCを注入後、23
℃で3日間放置した後、水の味の官能試験を行なった。
1+, the taste evaluation is based on the same packaging as the odor evaluation;
After pouring 200cc of mineral water into it, 23
After standing for 3 days at ℃, a sensory test of the taste of the water was conducted.

評価は、7人のパネラ−の評点の平均値を取り、その点
(0・・・全熱感じない、1・・・弱く感じる、2・・
・はっきり感じる、3・・・強く感じる)をもって、0
を◎、0〜1を01〜2をΔ、2〜3を×で表わした。
The evaluation is based on the average score of the seven panelists, and the score is 0: I don't feel any heat, 1: I feel it weak, 2...
・I feel it clearly, 3...I feel it strongly), and 0
◎, 0 to 1, 01 to 2, Δ, and 2 to 3, ×.

(発明の効果) 第1表からも分かる通り、本願発明の積層体は、基材や
接着剤に起因する臭いや味の移行を防止する顕著な効果
を有するものであり、かつ簡易に包装材料としうるもの
で、実用価値の高いものである。
(Effects of the Invention) As can be seen from Table 1, the laminate of the present invention has a remarkable effect of preventing the transfer of odors and tastes caused by base materials and adhesives, and can be easily applied to packaging materials. It is of high practical value.

(以下余白) □〇・(Margin below) □〇・

Claims (1)

【特許請求の範囲】[Claims] 23℃乾燥下での酸素透過量が50c.c./m^2・
24hr・atm以下のガスバリヤー性樹脂と実質的に
無臭のポリオレフィン系樹脂を140〜290℃で共押
出し成形し、次いで該ガスバリヤー性樹脂層を基材と積
層させた積層物において、該ガスバリヤー性樹脂層の厚
みが1〜30μで該ポリオレフィン系樹脂層が10〜2
00μであることを特徴とする積層体。
Oxygen permeation amount under drying at 23°C is 50c. c. /m^2・
In a laminate in which a gas barrier resin of 24 hr/atm or less and a substantially odorless polyolefin resin are coextruded at 140 to 290°C, and then the gas barrier resin layer is laminated with a base material, the gas barrier The thickness of the polyolefin resin layer is 1 to 30μ, and the thickness of the polyolefin resin layer is 10 to 2μ.
A laminate characterized by having a thickness of 00μ.
JP59229660A 1984-10-31 1984-10-31 Laminate Granted JPS61108549A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59229660A JPS61108549A (en) 1984-10-31 1984-10-31 Laminate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59229660A JPS61108549A (en) 1984-10-31 1984-10-31 Laminate

Publications (2)

Publication Number Publication Date
JPS61108549A true JPS61108549A (en) 1986-05-27
JPH0463776B2 JPH0463776B2 (en) 1992-10-12

Family

ID=16895679

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59229660A Granted JPS61108549A (en) 1984-10-31 1984-10-31 Laminate

Country Status (1)

Country Link
JP (1) JPS61108549A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS633950A (en) * 1986-05-16 1988-01-08 インタ−ナシヨナル ペ−パ− コンパニ− Heat sealable partition wall material for improved juice packaging
JPS63312143A (en) * 1987-05-29 1988-12-20 インターナショナル ペーパー コンパニー Improved non-foil composite structure for packaging juice
JPH04234645A (en) * 1990-12-20 1992-08-24 Westvaco Corp Paperboard container and manufacture thereof
US5164267A (en) * 1989-05-24 1992-11-17 Solvay & Cie (Societe Anonyme) Laminated composite
JPH05138828A (en) * 1990-12-20 1993-06-08 Westvaco Corp Paperboard container and its preparation
CN1058452C (en) * 1996-03-04 2000-11-15 南亚塑胶工业股份有限公司 Process for producing composite plastic coating by thermal plastic polyolefin resin and ethylene-vinyl acetate copolymer

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5145184A (en) * 1974-10-15 1976-04-17 Dainippon Printing Co Ltd KAMIKATSUPUSEIKEIYOYONSOSEKISOFUIRUMU
JPS5363484A (en) * 1976-11-18 1978-06-06 Nippon Synthetic Chem Ind Co Ltd:The Multilayer structure
JPS5511820A (en) * 1978-07-10 1980-01-28 Mitsubishi Petrochemical Co Laminate polyolefine sheet of high transparency
JPS57178856A (en) * 1981-04-30 1982-11-04 Dainippon Printing Co Ltd Laminating material for extruding tube

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5145184A (en) * 1974-10-15 1976-04-17 Dainippon Printing Co Ltd KAMIKATSUPUSEIKEIYOYONSOSEKISOFUIRUMU
JPS5363484A (en) * 1976-11-18 1978-06-06 Nippon Synthetic Chem Ind Co Ltd:The Multilayer structure
JPS5511820A (en) * 1978-07-10 1980-01-28 Mitsubishi Petrochemical Co Laminate polyolefine sheet of high transparency
JPS57178856A (en) * 1981-04-30 1982-11-04 Dainippon Printing Co Ltd Laminating material for extruding tube

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS633950A (en) * 1986-05-16 1988-01-08 インタ−ナシヨナル ペ−パ− コンパニ− Heat sealable partition wall material for improved juice packaging
JP2583047B2 (en) * 1986-05-16 1997-02-19 インタ−ナシヨナル ペ−パ− コンパニ− Heat sealable barrier material for improved use packaging
JPS63312143A (en) * 1987-05-29 1988-12-20 インターナショナル ペーパー コンパニー Improved non-foil composite structure for packaging juice
JPH0572868B2 (en) * 1987-05-29 1993-10-13 Int Paper Co
US5164267A (en) * 1989-05-24 1992-11-17 Solvay & Cie (Societe Anonyme) Laminated composite
JPH04234645A (en) * 1990-12-20 1992-08-24 Westvaco Corp Paperboard container and manufacture thereof
JPH05138828A (en) * 1990-12-20 1993-06-08 Westvaco Corp Paperboard container and its preparation
JPH0655486B2 (en) * 1990-12-20 1994-07-27 ウェストヴァコ コーポレイション Paperboard container and manufacturing method thereof
JPH0655485B2 (en) * 1990-12-20 1994-07-27 ウェストヴァコ コーポレイション Paperboard container and manufacturing method thereof
CN1058452C (en) * 1996-03-04 2000-11-15 南亚塑胶工业股份有限公司 Process for producing composite plastic coating by thermal plastic polyolefin resin and ethylene-vinyl acetate copolymer

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