JPH0770341A - Polyester film for three-piece-can coating - Google Patents

Polyester film for three-piece-can coating

Info

Publication number
JPH0770341A
JPH0770341A JP22140493A JP22140493A JPH0770341A JP H0770341 A JPH0770341 A JP H0770341A JP 22140493 A JP22140493 A JP 22140493A JP 22140493 A JP22140493 A JP 22140493A JP H0770341 A JPH0770341 A JP H0770341A
Authority
JP
Japan
Prior art keywords
polyester
coated
film
piece
coating
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
JP22140493A
Other languages
Japanese (ja)
Other versions
JP3298712B2 (en
Inventor
Masashi Chiisako
雅司 竪
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.)
Diafoil Co Ltd
Original Assignee
Diafoil 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
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Application filed by Diafoil Co Ltd filed Critical Diafoil Co Ltd
Priority to JP22140493A priority Critical patent/JP3298712B2/en
Publication of JPH0770341A publication Critical patent/JPH0770341A/en
Application granted granted Critical
Publication of JP3298712B2 publication Critical patent/JP3298712B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To obtain a hygienically excellent three-piece can which is reduced in the amount of substances extractable with water or hot water. CONSTITUTION:The film, when used as a can coating formed by laminating to a metal with an adhesive, has a terminal carboxyl content lower than 50eq/t and a content of low-mol.wt. substances extracted by 1-hr retortion with 125 deg.C pure water of 2.0mug or lower per cm<2> of the coating.

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3ピース缶に被覆するた
めのポリエステルフィルムに関する。
FIELD OF THE INVENTION This invention relates to polyester films for coating three-piece cans.

【0002】[0002]

【従来の技術および発明が解決しようとする課題】近
年、熱可塑性樹脂フィルムを金属板に被覆して金属缶用
材料として使用する例が増加している。従来の金属板に
熱硬化性樹脂塗料を塗装、焼き付け硬化させる塗装板で
は、たとえ塗料の塗布量を多くしたり、ダブルコートを
行ってもピンホールなどによる金属露出を完全になくす
ことが困難であるのに対して、熱可塑性樹脂を被覆した
被覆金属板の場合、ほぼ完全に金属露出をなくすことが
できるからである。また、塗装板の場合、塗料の塗布お
よび乾燥焼き付けで大量の溶剤を使用するのに対して、
予め印刷を施した被覆用フィルムをラミネートすること
で印刷層を設けることができるからである。そして、こ
れら被覆に用いられる熱可塑性樹脂として、耐熱性、加
工性、ガスバリヤー性などに優れたポリエステルが一般
に用いられている。
2. Description of the Related Art In recent years, the number of cases in which a thermoplastic resin film is coated on a metal plate and used as a material for a metal can is increasing. It is difficult to completely eliminate metal exposure due to pinholes, etc., even with a large amount of paint applied or double coating with a coated plate in which a thermosetting resin paint is applied to a conventional metal plate and baked and cured. On the other hand, in the case of a coated metal plate coated with a thermoplastic resin, metal exposure can be almost completely eliminated. Also, in the case of coated plates, a large amount of solvent is used for coating and dry baking,
This is because the printing layer can be provided by laminating a coating film that has been printed in advance. As the thermoplastic resin used for these coatings, polyester having excellent heat resistance, processability, gas barrier properties, etc. is generally used.

【0003】プラスチック容器、延伸フィルムの原料と
して広く用いられているポリエチレンテレフタレート
は、かかる金属被覆用熱可塑性樹脂として耐熱性、加工
性、ガスバリヤー性等に優れており、いわゆるPETボ
トルなどのように飲料容器の構造体としても用いられて
いる。ところが、金属缶に被覆して用いられる場合、P
ETボトルなどの場合とは異なり、実質的に水である液
状内容物に接触した状態で殺菌などの目的で加圧高温下
に置かれることがある。この場合、いわゆるレトルト処
理を施された形となりオリゴマーやアルデヒドのような
低分子量物が液状内容物中に抽出されて出てくる可能性
があり、充填された内容物の風味が損なわれる恐れがあ
り、衛生上も好ましくなかった。
Polyethylene terephthalate, which is widely used as a raw material for plastic containers and stretched films, has excellent heat resistance, processability, gas barrier properties and the like as such a thermoplastic resin for metal coating, and is used like so-called PET bottles. It is also used as a structure for beverage containers. However, when it is used by coating it on a metal can, P
Unlike the case of an ET bottle or the like, it may be placed under high temperature under pressure for the purpose of sterilization or the like while being in contact with a liquid content that is substantially water. In this case, a so-called retort-treated form may be formed, and low molecular weight substances such as oligomers and aldehydes may be extracted into the liquid content and come out, and the flavor of the filled content may be impaired. Yes, it was not good for hygiene.

【0004】[0004]

【課題を解決するための手段】かかる問題点を解消すべ
く検討の結果、本発明に到達したものである。すなわ
ち、本発明の要旨は、接着剤で金属にラミネート被覆・
製缶された後の末端カルボキシル基濃度が50当量/t
未満であり、かつ、接着剤で金属にラミネート被覆・製
缶された後に125℃の純水で1時間のレトルト処理に
よって抽出される低分子量物が被覆表面1cm2 当たり
2.0μg以下であることを特徴とする3ピース缶被覆
用ポリエステルフィルムに存する。
The present invention has been achieved as a result of a study for solving such a problem. That is, the gist of the present invention is to laminate and coat metal with an adhesive.
The terminal carboxyl group concentration after can making is 50 equivalent / t.
Less and less than 2.0 μg per 1 cm 2 of coated surface, which is extracted by a retort treatment with pure water at 125 ° C. for 1 hour after laminating and canning a metal with an adhesive. And a polyester film for covering a three-piece can.

【0005】以下、本発明を詳細に説明する。本発明で
いう3ピース缶とは、例えば特開平5−69485号公
報に記載されている方法によって、溶接接合された金属
露出部が接着剤などによらず被覆フィルムによって融着
被覆された缶胴、フィルム被覆鋼板から内容物と接触す
る側が被覆層となるようにして缶蓋、缶底が構成されて
なるものである。かかる用途に用いられる金属板として
は表面処理鋼板、アルミニウム等の軽金属板等が挙げら
れる。表面処理鋼板の場合、一般的なクロム処理により
不動態化した錫で被覆したり、あるいはニッケル、亜鉛
のメッキ鋼等が挙げられる。特にクロム金属と酸化クロ
ムの2層を有する電解クロム被覆鋼は好適である。ま
た、アルミニウムの場合、純アルミニウムでもよいが、
マンガン、マグネシウム、亜鉛、銅等が若干量含有され
る合金であってもよい。また、純アルミニウム、アルミ
ニウム合金いずれもクロム酸処理あるいはクロム酸/燐
酸処理が行われていてもよい。
The present invention will be described in detail below. The three-piece can referred to in the present invention is, for example, a can body in which a metal exposed portion welded and joined is fusion-coated with a coating film by a method described in JP-A-5-69485 without using an adhesive or the like. The can lid and the can bottom are configured such that the side of the film-coated steel sheet that comes into contact with the contents is the coating layer. Examples of the metal plate used for such an application include a surface-treated steel plate and a light metal plate such as aluminum. In the case of the surface-treated steel sheet, examples thereof include coating with tin that has been passivated by a general chrome treatment, or nickel- or zinc-plated steel. In particular, electrolytic chromium-coated steel having two layers of chromium metal and chromium oxide is preferable. In the case of aluminum, pure aluminum may be used,
It may be an alloy containing a small amount of manganese, magnesium, zinc, copper or the like. Further, both pure aluminum and aluminum alloy may be treated with chromic acid or chromic acid / phosphoric acid.

【0006】本発明いうポリエステルとは、二官能性酸
成分として芳香族ジカルボン酸またはそのエステル形成
誘導体、具体的にはテレフタル酸、イソフタル酸、フタ
ル酸、2,6−ナフタレンジカルボン酸、セバシン酸、
アジピン酸等、またはそのエステル形成誘導体の1種以
上と、グリコール成分としてエチレングリコール、ジエ
チレングリコール、トリエチレングリコール、1,3−
プロパンジオール、1,4−ブタンジオール、1,4−
シクロヘキサンジメタノール等の1種もしくは2種以上
とからなるポリエステルが好適に挙げられる。代表的な
ポリエステルとしてはポリエチレンテレフタレートとそ
の共重合体、ポリエチレン2,6−ナフタレンジカルボ
キシレートとその共重合体、ポリシクロヘキサンジメチ
レンテレフタレートとその共重合体等が例示される。
The polyester referred to in the present invention means an aromatic dicarboxylic acid or its ester-forming derivative as a difunctional acid component, specifically, terephthalic acid, isophthalic acid, phthalic acid, 2,6-naphthalenedicarboxylic acid, sebacic acid,
Adipic acid or the like, or one or more kinds of ester-forming derivatives thereof, and ethylene glycol, diethylene glycol, triethylene glycol, 1,3-as a glycol component.
Propanediol, 1,4-butanediol, 1,4-
Preferable are polyesters composed of one kind or two or more kinds such as cyclohexanedimethanol. Examples of typical polyesters include polyethylene terephthalate and its copolymers, polyethylene 2,6-naphthalene dicarboxylate and its copolymers, polycyclohexane dimethylene terephthalate and its copolymers, and the like.

【0007】本発明のポリエステルフィルムは通常、前
述ポリエステルからなり、二軸延伸や熱固定が施された
ものであって、面配向度(ΔP)が少なくとも0.10
0〜0.200、さらに0.110〜0.190、特に
0.130〜0.180ものが好ましく、結晶化度χc
が少なくとも30〜70%、さらに35〜60%、特に
40〜60%のものが好ましい。ΔPが0.100未満
である場合、十分なガスバリヤー性が得られない傾向が
ある。同様にχc が30%未満である場合、十分なガス
バリヤー性が得られない傾向がある。ΔPが0.200
を超える場合、あるいはχc が70%を超える場合、フ
ィルムの剛性が高くなりすぎて金属板にラミネートした
後、成形加工し製缶するに際してフィルムが金属板から
剥離したり、フィルムにクラックが入ったり、金属缶と
した後の耐デント性が低下したりすることがある。
The polyester film of the present invention is usually made of the above polyester and is biaxially stretched or heat-set, and has a degree of plane orientation (ΔP) of at least 0.10.
0 to 0.200, more preferably 0.110 to 0.190, and particularly preferably 0.130 to 0.180, the crystallinity χc
Is preferably at least 30 to 70%, more preferably 35 to 60%, and particularly preferably 40 to 60%. When ΔP is less than 0.100, sufficient gas barrier properties tend not to be obtained. Similarly, when χc is less than 30%, sufficient gas barrier properties tend not to be obtained. ΔP is 0.200
When the value exceeds 50% or when χc exceeds 70%, the film becomes too rigid and is laminated on a metal plate, then the film peels from the metal plate or is cracked when forming and forming a can. However, the dent resistance of the metal can may decrease after it is formed.

【0008】本発明のポリエステルフィルムには、通
常、フィルム内部に含有されるフィラーを核とする表面
突起が多数形成されており、動摩擦係数μd は0.02
〜0.50、さらに0.05〜0.45、特に0.07
〜0.40が好ましい。μd が0.02未満である場
合、表面の凹凸が増加する傾向があり、外観を損ねる恐
れがある。μd が0.50を超える場合、製缶工程でフ
ィルムが被覆された部分同士が接触したときにブロッキ
ングを起こしやすくなる傾向がある。
The polyester film of the present invention is usually formed with a large number of surface protrusions whose core is a filler contained in the film and has a dynamic friction coefficient μd of 0.02.
~ 0.50, more preferably 0.05-0.45, especially 0.07
~ 0.40 is preferred. When μd is less than 0.02, surface irregularities tend to increase, and the appearance may be impaired. When μd exceeds 0.50, blocking tends to occur when the film-covered portions come into contact with each other in the can-making process.

【0009】本発明のポリエステルフィルムの最大の特
徴はラミネート被覆金属缶としたときに末端カルボキシ
ル基濃度が低く、かつ水やエタノール水溶液に浸漬、加
熱して抽出されてくる低分子量物量が極めて少ないこと
である。すなわち、接着剤で金属にラミネート被覆・製
缶された後の末端カルボキシル基濃度が50当量/t未
満、好ましくは40当量/t未満、さらに好ましくは3
0当量/t未満である。末端カルボキシル基濃度が50
当量/tを超えると、熱劣化分解の開始点となる末端カ
ルボキシル基が多くなり過ぎるため、被覆製缶された後
に加熱されると新たに低分子量物が生成するので好まし
くない。また、接着剤で金属にラミネート被覆・製缶さ
れた後に125℃の純水で1時間レトルト処理を施して
抽出される低分子量物がポリエステル被覆金属1cm2
当たり2.0μg以下、好ましくは1.5μg以下、さ
らに好ましくは1.0μg以下である。かかるレトルト
処理で抽出される低分子量物がポリエステル被覆金属1
cm2 当たり2.0μgを超えると、殺菌などの目的で
加熱されたとき充填された内容物の風味が損なわれ、衛
生上も好ましくない。
The greatest feature of the polyester film of the present invention is that the concentration of terminal carboxyl groups is low when a laminated coated metal can is used, and the amount of low molecular weight substances extracted by immersion in water or an aqueous ethanol solution and heating is extremely small. Is. That is, the terminal carboxyl group concentration after the metal is laminated and coated with an adhesive to form a can is less than 50 equivalents / t, preferably less than 40 equivalents / t, further preferably 3
It is less than 0 equivalent / t. Terminal carboxyl group concentration is 50
If it exceeds the equivalent weight / t, the number of terminal carboxyl groups, which are the starting points of thermal degradation decomposition, becomes too large, so that a new low molecular weight substance is newly formed when heated after the coating can is not preferable. In addition, a low molecular weight substance extracted by applying a retort treatment with pure water at 125 ° C for 1 hour after being laminated and metal-coated on a metal with an adhesive is a polyester-coated metal 1 cm 2
The amount is 2.0 μg or less, preferably 1.5 μg or less, and more preferably 1.0 μg or less. The low molecular weight substance extracted by such retort treatment is polyester-coated metal 1
When it exceeds 2.0 μg per cm 2 , the flavor of the filled contents is impaired when heated for the purpose of sterilization and the like, which is not preferable in terms of hygiene.

【0010】レトルト処理で抽出される低分子量物量を
低減化させる方法として、1)重縮合に際して固相重合
により低分子量物の内在量を低減したポリエステルから
ポリエステルフィルムを構成する、2)重縮合して得ら
れたポリエステルレジンに予め温水による浸漬処理を施
して低分子量物の内在量を低減したポリエステルからポ
リエステルフィルムを構成する、3)常法で得られたポ
リエステルフィルムに温水浸漬処理を施して低分子量物
の内在量を低減化する等の方法が挙げられ、これら方法
を単独あるいは複数を組み合わせて本発明のポリエステ
ルフィルムを得る。さらに各方法を実例を示して説明す
る。固相重合によって低分子量物を低減化する方法は、
通常のポリエステルの製造において、極限粘度[η]が
0.60以上になるまで重合が行われているところを、
0.40〜0.50で重合を停止し、得られたレジンを
0.3mmHgの高真空下で240℃で10時間加熱す
る。
As a method for reducing the amount of low molecular weight substances extracted by the retort treatment, 1) a polyester film is formed from polyester in which the internal amount of low molecular weight substances is reduced by solid-state polymerization during polycondensation, 2) polycondensation The polyester resin obtained in this way is preliminarily soaked in warm water to form a polyester film from a polyester having a reduced amount of low molecular weight substances. 3) The polyester film obtained by a conventional method is soaked in warm water to reduce Examples thereof include a method of reducing the intrinsic amount of the molecular weight substance, and these methods may be used alone or in combination to obtain the polyester film of the present invention. Further, each method will be described by showing an actual example. A method for reducing low molecular weight substances by solid phase polymerization is
In the usual polyester production, where polymerization is carried out until the intrinsic viscosity [η] becomes 0.60 or more,
The polymerization is stopped at 0.40 to 0.50, and the obtained resin is heated at 240 ° C. for 10 hours under a high vacuum of 0.3 mmHg.

【0011】ポリエステルを予め温水浸漬処理を施して
低分子量物の内在量を低減化する方法は、ポリエステル
を水、水蒸気、水蒸気含有不活性ガス、水蒸気含有空気
などと接触させることにより行われる。ポリエステルは
室温〜150℃の水に1分間〜100時間またはそれ以
上、好ましくは1分間〜20時間、さらに好ましくは5
分〜10時間浸漬することによって行われる。望ましく
は、ポリエステルを50〜150℃の熱水に1分間〜1
0時間浸漬することにより行われる。さらに望ましくは
ポリエステルを70〜110℃の熱水に3分〜5時間浸
漬することにより行われる。特に好ましくは、ポリエス
テルを80〜100℃の熱水に5分間〜3時間浸漬する
ことにより行われる。
The method of preliminarily dipping the polyester in hot water to reduce the amount of the low molecular weight substances present is carried out by bringing the polyester into contact with water, steam, a steam-containing inert gas, steam-containing air or the like. The polyester is immersed in water at room temperature to 150 ° C. for 1 minute to 100 hours or more, preferably 1 minute to 20 hours, more preferably 5 minutes.
It is performed by immersing for 10 minutes to 10 minutes. Desirably, the polyester is heated in hot water at 50 to 150 ° C. for 1 minute to 1
It is performed by soaking for 0 hour. More desirably, the polyester is immersed in hot water at 70 to 110 ° C. for 3 minutes to 5 hours. Particularly preferably, it is carried out by immersing the polyester in hot water at 80 to 100 ° C. for 5 minutes to 3 hours.

【0012】また、ポリエステルと水蒸気または水蒸気
含有ガスあるいは水蒸気含有空気との接触は、通常、室
温〜150℃、好ましくは50〜150℃、さらに好ま
しくは70〜110℃の温度の水蒸気または水蒸気含有
ガスあるいは水蒸気含有空気を好ましくはポリエステル
1kg当たり、0.5g以上の量で供給させるか、ある
いは存在させてポリエステルと水蒸気とを接触させるこ
とにより行われる。このポリエステルと水蒸気との接触
は通常、1分間〜50時間、好ましくは5分間〜10時
間行われる。ポリエステルフィルムに温水浸漬処理を施
して低分子量物の内在量を低減化する方法は、前述のポ
リエステルレジンに施した温水浸漬処理に準ずる。本発
明のポリエステルフィルムは常法に従って製造するが、
以下にその一例を示す。
The contact between the polyester and the steam or the steam-containing gas or the steam-containing air is usually room temperature to 150 ° C., preferably 50 to 150 ° C., more preferably 70 to 110 ° C. Alternatively, the steam-containing air is preferably supplied in an amount of 0.5 g or more per 1 kg of polyester, or is allowed to exist and the polyester and steam are brought into contact with each other. The contact between the polyester and steam is usually performed for 1 minute to 50 hours, preferably 5 minutes to 10 hours. The method of subjecting the polyester film to the hot water immersion treatment to reduce the internal content of the low molecular weight substance is similar to the warm water immersion treatment applied to the polyester resin. The polyester film of the present invention is produced according to a conventional method,
An example is shown below.

【0013】まず、原料ポリエステルを溶融押出法で実
質的に無定形であるシートを得る。この時に熱劣化によ
る低分子量物内在量の増加を抑えるために少なくとも3
00℃以下、好ましくは290℃以下、さらに好ましく
は280℃以下の溶融温度で、長くとも15分間、好ま
しくは10分間、さらに好ましくは5分間の滞留時間と
なるように溶融押出する。得られた無定形シートをロー
ル延伸機を用いてポリエステルのガラス転移点〜160
℃の温度で縦方向に延伸する。得られた一軸延伸フィル
ムに各種印刷性向上のための塗布液塗布する。さらにテ
ンター延伸機を用いて縦方向延伸温度〜170℃の温度
で塗布液を乾燥、架橋重合させながら横方向に延伸し、
引き続きテンター内で100〜240℃の温度で熱処理
を施し、二軸延伸フィルムを得る。要すればさらにロー
ル延伸機、テンター延伸機を用いてそれぞれ再縦延伸、
再横延伸を施す。
First, a raw material polyester is melt-extruded to obtain a substantially amorphous sheet. At this time, in order to suppress the increase in the amount of the low molecular weight substance contained due to heat deterioration, at least 3
Melt extrusion is performed at a melting temperature of 00 ° C. or lower, preferably 290 ° C. or lower, more preferably 280 ° C. or lower, for a residence time of at most 15 minutes, preferably 10 minutes, more preferably 5 minutes. The obtained amorphous sheet was stretched by a roll stretching machine at a glass transition point of polyester up to 160.
Stretching in the machine direction at a temperature of ° C. The obtained uniaxially stretched film is coated with a coating liquid for improving various printability. Further, using a tenter stretching machine, the coating liquid is dried at a temperature of from the longitudinal stretching temperature to 170 ° C. and stretched in the transverse direction while being crosslinked and polymerized,
Subsequently, heat treatment is performed in a tenter at a temperature of 100 to 240 ° C. to obtain a biaxially stretched film. If necessary, a roll stretching machine and a tenter stretching machine are used to respectively re-longitudinal stretching,
Re-transverse stretching is performed.

【0014】本発明のポリエステルフィルムを被覆した
3ピース缶の製造方法についての一例を示す。3ピース
缶には缶胴の接合方法の違いによって、はんだ缶、接着
缶、溶接缶に大別されるが、本発明のポリエステルフィ
ルムは特に接着缶、溶接缶に対して好適である。接着缶
は一般缶では古くから用いられており、はぜ折りした部
分に溶融した接着剤を注入する方法である。溶接缶の製
法としてはコノウェルド法、スードロニックウェルド法
が挙げられるが、前者はTFS(Tin Free St
eel)表面のクロム皮膜を剥離し、ロール電極によっ
て鋼母材を溶接する方法である。後者はブリキを対象と
したもので、ブランクの溶接端面を研磨せずに、銅ワイ
ヤーをロール電極とブリキの間の中間電極として使用し
て溶接する方法である。
An example of a method for producing a three-piece can coated with the polyester film of the present invention will be shown. Three-piece cans are roughly classified into solder cans, adhesive cans, and welded cans depending on the method of joining the can bodies, and the polyester film of the present invention is particularly suitable for adhesive cans and welded cans. Adhesive cans have been used for a long time in general cans, and are a method of injecting a molten adhesive into a folded portion. As a manufacturing method of a welding can, a cono weld method and a sudronic weld method can be mentioned. The former is TFS (Tin Free St).
eel) A method of peeling off the chromium film on the surface and welding the steel base material with a roll electrode. The latter is intended for tinplate, and is a method of welding by using a copper wire as an intermediate electrode between the roll electrode and the tinplate without polishing the weld end surface of the blank.

【0015】まず、3ピース缶を構成するポリエステル
被覆鋼板を製造する。本発明のポリエステルフィルムを
各種接着剤、例えばエポキシ樹脂接着剤を用いてクロム
表面処理鋼板や錫メッキ鋼板あるいはアルミニウム板の
両面に加圧接着する。このとき、缶胴とするための鋼板
には事前に各種の印刷を施した本発明のフィルムを被覆
してもよい。ポリエステルが被覆されたクロム表面処理
鋼板、錫メッキ鋼板は缶胴、缶底の原材料として、ポリ
エステルが被覆されたアルミニウム板は缶蓋の原材料と
して用いられる。いずれの場合も適当な形に切り抜き3
ピース缶の構成部品として用いる。まず、缶胴用被覆鋼
板を筒状に丸め、上記の接合方法によって缶胴とする。
この缶胴に缶底用被覆鋼板を取り付けるが、缶胴の巻き
込み縁部に密封材料としてゴム系のシーリングコンパウ
ンドを塗布乾燥して缶底を二重に巻き締める。通常はこ
のようにして得られた成形体にジュースなどの内容物を
充填した後に缶底同様にして缶蓋用ポリエステル被覆ア
ルミニウム板を巻き締め3ピース缶とする。
First, a polyester-coated steel sheet forming a three-piece can is manufactured. The polyester film of the present invention is pressure-bonded to both surfaces of a chrome surface-treated steel plate, a tin-plated steel plate or an aluminum plate by using various adhesives such as epoxy resin adhesives. At this time, the steel plate for forming the can body may be coated with the film of the present invention which has been subjected to various printings in advance. Chromium surface-treated steel sheets and tin-coated steel sheets coated with polyester are used as raw materials for the can body and the bottom of the can, and aluminum sheets coated with polyester are used as raw materials for the can lid. In any case, cut out to a suitable shape 3
Used as a component of a piece can. First, the coated steel sheet for a can body is rolled into a tubular shape, and the can body is made by the above-mentioned joining method.
A coated steel plate for a can bottom is attached to this can body. A rubber-based sealing compound is applied as a sealing material to the winding edge of the can body and dried to double-tighten the can bottom. Usually, the molded body thus obtained is filled with contents such as juice and then a polyester-coated aluminum plate for a can lid is wound in the same manner as the can bottom to form a three-piece can.

【0016】[0016]

【実施例】以下、本発明を実施例を挙げてさらに詳細に
説明するが、本発明の要旨を越えない限り、以下の実施
例によって限定されるものではない。なお、実施例中の
評価方法は下記のとおりである。実施例および比較例
中、「部」とあるのは「重量部」を示す。 (1)極限粘度[η] ポリマー1gをフェノール/テトラクロロエタン=50
/50(重量比)の混合溶媒100ml中に溶解し、3
0℃で測定した。
EXAMPLES The present invention will be described in more detail with reference to examples, but the invention is not limited to the following examples without departing from the gist of the invention. The evaluation methods in the examples are as follows. In Examples and Comparative Examples, "part" means "part by weight". (1) Intrinsic viscosity [η] 1 g of a polymer was added to phenol / tetrachloroethane = 50
Dissolve in 100 ml of a mixed solvent of 50/50 (weight ratio) and
It was measured at 0 ° C.

【0017】(2)低分子量抽出物量(μg/cm2) 試料フィルムをエポキシ樹脂接着剤を用いてクロムメッ
キ処理を施した厚み0.30mmの鋼板に加圧接着して
ポリエステル被覆鋼板を得た。ただし、樹脂が被覆され
ているのは鋼板の片面だけとした。ポリエステルが被覆
されている面を内側とするようにして、特開平5−69
485号公報に開示されている方法によって、溶接接合
された金属露出部が接着剤などによらず被覆フィルムに
よって融着被覆された350mlのジュース缶胴を製造
し、また別途前述のポリエステル被覆鋼板から内容物と
接触する側が被覆層となるようにして缶蓋、缶底を製造
した。これら缶胴、缶蓋、缶底よりなる3ピース缶を製
造し内部に純水300mlを封入した。このポリエステ
ル被覆3ピース缶を125℃となるよう加熱して1時間
レトルト処理を行う。レトルト処理後の水を回収し、水
を留去し得られた不揮発物の質量M(μg)を測定し、
用いた試料3ピース缶の内部表面積S(cm2 )で除し
た値M/S(μg/cm2 )を低分子量抽出物量とす
る。
(2) Low molecular weight extract amount (μg / cm 2) A sample film was pressure-bonded to a 0.30 mm-thick steel plate plated with chromium using an epoxy resin adhesive to obtain a polyester-coated steel plate. However, the resin was coated only on one side of the steel sheet. The surface coated with polyester is set to be the inner side, and the method is disclosed in JP-A-5-69.
According to the method disclosed in Japanese Patent Publication No. 485, a 350 ml juice can body in which a metal exposed portion welded and joined is fusion-coated with a coating film without using an adhesive or the like is manufactured. A can lid and a can bottom were manufactured so that the side in contact with the contents was the coating layer. A three-piece can consisting of the can body, the can lid, and the can bottom was manufactured, and 300 ml of pure water was sealed inside. This polyester-coated 3-piece can is heated to 125 ° C. and subjected to retort treatment for 1 hour. The water after the retort treatment is recovered, the water is distilled off, and the mass M (μg) of the obtained non-volatile matter is measured.
The value M / S (μg / cm 2 ) divided by the internal surface area S (cm 2 ) of the sample three-piece can used is taken as the amount of low molecular weight extract.

【0018】(3)抽出外観 レトルト処理後の水を回収しキセノン灯を光源としてチ
ンダル現象の観察を行い、次の基準に従ってランク付け
をした。 ◎:レトルト直後および1週間静置後のいずれでも光路
の濁りは観察されない ○:レトルト直後に光路の濁りは観察されず、1週間静
置後室内光程度の光量下では透明だが、キセノン光路に
はチンダル現象が観察される △:レトルト直後に室内光程度の光量下では透明だが、
キセノン光路にはチンダル現象が観察され、1週間静置
後は室内光下でも肉眼で水中浮遊物が観察される ×:レトルト直後および1週間静置後のいずれでも室内
光下で肉眼にて水中浮遊物が観察される
(3) Appearance of extraction The water after the retort treatment was recovered, and the Tyndall phenomenon was observed using a xenon lamp as a light source, and ranked according to the following criteria. ◎: No turbidity of the optical path was observed immediately after the retort or after standing for 1 week. ○: No turbidity of the optical path was observed immediately after the retort. Indicates a Tyndall phenomenon. △: Immediately after the retort, it is transparent under the amount of room light, but
Tyndall phenomenon is observed in the xenon optical path, and underwater light is visually observed even under room light after standing for 1 week. ×: Underwater under room light under naked light, both immediately after retort and after standing for 1 week. Floating matter is observed

【0019】(4)末端カルボキシル基濃度(当量/
t) Makromol.chem.,26,226(195
8)に記載のA.Conixの方法に従って測定した。 (5)面配向度(ΔP) アタゴ光学社製アッベ式屈折計を用い、フィルム面内の
屈折率の最大値aと最小値b、およびフィルム厚さ方向
の屈折率cを測定し、次式により面配向を算出した。な
お、屈折率の測定は、ナトリウムD線を用い、23℃5
0RH%雰囲気下で行った。 ΔP=(a+b)/2 − c
(4) Terminal carboxyl group concentration (equivalent /
t) Makromol. chem. , 26, 226 (195
A. described in 8). It was measured according to the method of Conix. (5) Degree of plane orientation (ΔP) The maximum value a and the minimum value b of the refractive index in the film plane and the refractive index c in the film thickness direction are measured using an Abbe refractometer manufactured by Atago Optical Co., Ltd. The plane orientation was calculated by. In addition, the measurement of the refractive index uses a sodium D line at 23 ° C. 5
It was performed under 0RH% atmosphere. ΔP = (a + b) / 2−c

【0020】(6)結晶化度χc (%) n−ヘプタン、四塩化炭素の混合液で、密度勾配ができ
ている密度勾配間に標準密度のフロートを入れ、そのフ
ロートに対し、試料がどの位置にあるかで試料の密度ρ
とした。得られた密度ρを次式に代入し、結晶化度χc
を得た。
(6) Crystallinity χ c (%) A mixed solution of n-heptane and carbon tetrachloride that has density gradients. A standard density float is placed between the density gradients, and the sample is Density ρ of sample depending on position
And Substituting the obtained density ρ into the following equation, the crystallinity χc
Got

【数1】χc =(ρ−1.335)×100/(1.4
55−1.335) (7)動摩擦係数μd 平滑なガラス板上に、幅15mm、長さ150mmに切
り出したフィルム同士を2枚重ね、その上にゴム板を載
せ、さらにその上に荷重を載せ、2枚のフィルムの接圧
を2g/cm2 として、20mm/minでフィルム同
士を滑らせて摩擦力を測定し、摩擦力を接圧で除し、さ
らに接触面積で除したものを摩擦係数とした。5mm滑
らせた点での摩擦係数を動摩擦係数μd とした。
## EQU1 ## χ c = (ρ-1.335) × 100 / (1.4
55-1.335) (7) Dynamic friction coefficient μd Two pieces of film cut into a width of 15 mm and a length of 150 mm are stacked on a smooth glass plate, a rubber plate is placed on it, and a load is further placed on it. With the contact pressure between the two films set to 2 g / cm 2 , the friction force was measured by sliding the films at 20 mm / min, the friction force was divided by the contact pressure, and the result was divided by the contact area. And The coefficient of friction at the point of sliding by 5 mm was defined as the dynamic coefficient of friction μd.

【0021】実施例1 [ポリエステルの製造] (ポリエステルa)テレフタル酸ジメチル100部、エ
チレングリコール60部および酢酸カルシウム一水塩
0.1部を反応器にとり、エステル交換反応を行った。
すなわち、反応開始温度を170℃とし、メタノールの
留出と共に徐々に反応温度を上昇させて4時間後に23
0℃まで昇温し、実質的にエステル交換反応を終了させ
た。次いで、平均粒径3μmの無定形酸化珪素を含有す
るエチレングリコールスラリーとリン酸0.04部を添
加した後、三酸化アンチモン0.04部を添加し、常法
により重縮合反応を行った。すなわち、温度を徐々に高
めると共に圧力を徐々に減じ、2時間後に温度は280
℃、圧力は0.3mmHgとし、さらに2時間経った時
点で反応を停止し、酸化珪素0.05部含有し、極限粘
度が0.62であるポリエステルを得た。
Example 1 [Production of polyester] (Polyester a) 100 parts of dimethyl terephthalate, 60 parts of ethylene glycol and 0.1 part of calcium acetate monohydrate were placed in a reactor to carry out a transesterification reaction.
That is, the reaction start temperature was set to 170 ° C., the reaction temperature was gradually raised with the distillation of methanol, and after 23 hours, 23
The temperature was raised to 0 ° C. to substantially end the transesterification reaction. Then, after adding ethylene glycol slurry containing amorphous silicon oxide having an average particle diameter of 3 μm and 0.04 part of phosphoric acid, 0.04 part of antimony trioxide was added, and polycondensation reaction was carried out by a conventional method. That is, the temperature is gradually increased and the pressure is gradually reduced, and after 2 hours, the temperature is 280
The temperature was set to 0 ° C. and the pressure to 0.3 mmHg, and the reaction was stopped after a lapse of 2 hours to obtain a polyester containing 0.05 part of silicon oxide and having an intrinsic viscosity of 0.62.

【0022】(ポリエステルb)テレフタル酸ジメチル
100部、エチレングリコール60部および酢酸カルシ
ウム一水塩0.1部を反応器にとり、エステル交換反応
を行った。すなわち、反応開始温度を170℃とし、メ
タノールの留出と共に徐々に反応温度を上昇させて4時
間後に230℃まで昇温し、実質的にエステル交換反応
を終了させた。次いで、平均粒径3μmの無定形酸化珪
素を含有するエチレングリコールスラリーとリン酸0.
07部を添加した後、三酸化アンチモン0.04部を添
加し、常法により重縮合反応を行った。すなわち、温度
を徐々に高めると共に圧力を徐々に減じ、2時間後に温
度は280℃、圧力は0.3mmHgとし、さらに1時
間班経った時点で反応を停止し、酸化珪素0.05部含
有し、極限粘度が0.45であるポリエステルを得た。
このポリエステルをさらに225℃、0.3mmHgで
10時間固相重合を施し、極限粘度[η]が0.75の
ポリエステルを得た。
(Polyester b) 100 parts of dimethyl terephthalate, 60 parts of ethylene glycol and 0.1 part of calcium acetate monohydrate were placed in a reactor and transesterified. That is, the reaction start temperature was set to 170 ° C., the reaction temperature was gradually raised along with the distillation of methanol, and the temperature was raised to 230 ° C. after 4 hours to substantially end the transesterification reaction. Then, an ethylene glycol slurry containing amorphous silicon oxide having an average particle diameter of 3 μm and phosphoric acid of 0.1.
After adding 07 parts, 0.04 part of antimony trioxide was added, and polycondensation reaction was carried out by a conventional method. That is, the temperature was gradually increased and the pressure was gradually decreased, and after 2 hours, the temperature was 280 ° C., the pressure was 0.3 mmHg, the reaction was stopped after 1 hour, and 0.05 part of silicon oxide was contained. A polyester having an intrinsic viscosity of 0.45 was obtained.
This polyester was further subjected to solid phase polymerization at 225 ° C. and 0.3 mmHg for 10 hours to obtain a polyester having an intrinsic viscosity [η] of 0.75.

【0023】(ポリエステルc)ポリエステルaを純水
が入った圧力容器中に入れ、内温を90℃にコントロー
ルし、4時間保持して浸漬処理を行った後、水を留去し
てポリエステルcを得た。
(Polyester c) Polyester a was placed in a pressure vessel containing pure water, the internal temperature was controlled at 90 ° C., the dipping treatment was carried out by holding for 4 hours, and then water was distilled off to give polyester c. Got

【0024】(ポリエステルd)ポリエステルbを純水
が入った圧力容器中に入れ、内温を90℃にコントロー
ルし、4時間保持して浸漬処理を行った後、水を留去し
てポリエステルdを得た。
(Polyester d) Polyester b is placed in a pressure vessel containing pure water, the internal temperature is controlled at 90 ° C., the temperature is maintained for 4 hours for immersion treatment, and then water is distilled off to produce polyester d. Got

【0025】(ポリエステルe)テレフタル酸ジメチル
78部、イソフタル酸ジメチル12部、エチレングリコ
ール60部および酢酸カルシウム一水塩0.1部を反応
器にとり、エステル交換反応を行った。すなわち、反応
開始温度を170℃とし、メタノールの留出と共に徐々
に反応温度を上昇させて4時間後に230℃まで昇温
し、実質的にエステル交換反応を終了させた。次いで、
平均粒径3μmの無定形酸化珪素を含有するエチレング
リコールスラリーとリン酸0.04部を添加した後、三
酸化アンチモン0.04部を添加し、常法により重縮合
反応を行った。すなわち、温度を徐々に高めると共に圧
力を徐々に減じ、2時間後に温度は280℃、圧力は
0.3mmHgとし、さらに2時間経った時点で反応を
停止し、酸化珪素0.05部含有し、極限粘度が0.7
0であるポリエステルを得た。
(Polyester e) 78 parts of dimethyl terephthalate, 12 parts of dimethyl isophthalate, 60 parts of ethylene glycol and 0.1 part of calcium acetate monohydrate were placed in a reactor for transesterification. That is, the reaction start temperature was set to 170 ° C., the reaction temperature was gradually raised along with the distillation of methanol, and the temperature was raised to 230 ° C. after 4 hours to substantially end the transesterification reaction. Then
After adding ethylene glycol slurry containing amorphous silicon oxide having an average particle diameter of 3 μm and 0.04 part of phosphoric acid, 0.04 part of antimony trioxide was added and polycondensation reaction was carried out by a conventional method. That is, the temperature is gradually increased and the pressure is gradually reduced, the temperature is 280 ° C. and the pressure is 0.3 mmHg after 2 hours, the reaction is stopped after 2 hours, and 0.05 part of silicon oxide is contained. Intrinsic viscosity is 0.7
A polyester of 0 was obtained.

【0026】[ポリエステルフィルムの製造]ポリエス
テルbを溶融押出法でTダイより280℃、滞留時間5
分で溶融押出した。Tダイより押し出した後、キャスト
ドラム上にてガラス転移点以下の温度まで急冷し、実質
的に無定形のシートを得た。このシートをロール延伸機
を用いて80℃で縦方向に3.6倍延伸した。次にテン
ター延伸機を用いて100℃で横方向に4.2倍延伸
し、引き続きテンター内にて230℃で熱固定を施し、
厚み25μmのフィルムを得た。 [3ピース缶の製造]得られたフィルムをエポキシ樹脂
接着剤を用いてクロムメッキ処理を施した厚み0.30
mmの鋼板に加圧接着し、ポリエステル被覆鋼板を得
た。ただし、樹脂が被覆されているのは鋼板の片面だけ
とした。ポリエステルが被覆されている面を内側とする
ようにして、特開平5−69485号公報に記載されて
いる方法によって、溶接接合された金属露出部が接着剤
などによらず被覆フィルムによって融着被覆された35
0mlのジュース缶胴を製造し、また別途前述のポリエ
ステル被覆鋼板から内容物と接触する側が被覆層となる
ようにして缶蓋、缶底を製造した。これらの缶胴、缶
蓋、缶底よりなる3ピース缶を製造した。
[Production of Polyester Film] Polyester b was melt-extruded from a T-die at 280 ° C. for a residence time of 5
Melt extruded in minutes. After being extruded from the T-die, it was rapidly cooled to a temperature below the glass transition point on a cast drum to obtain a substantially amorphous sheet. This sheet was stretched 3.6 times in the machine direction at 80 ° C. using a roll stretching machine. Next, it was stretched 4.2 times in the transverse direction at 100 ° C. using a tenter stretching machine, and subsequently heat-set at 230 ° C. in a tenter,
A film having a thickness of 25 μm was obtained. [Production of 3-piece can] Chromium plating of the obtained film using an epoxy resin adhesive, thickness 0.30
A polyester-coated steel plate was obtained by pressure-bonding to a mm steel plate. However, the resin was coated only on one side of the steel sheet. The exposed surface of the welded metal is fusion-coated with a coating film by the method described in JP-A-5-69485 so that the surface coated with polyester is the inside. 35
A 0 ml juice can barrel was manufactured, and a can lid and a can bottom were separately manufactured from the above polyester-coated steel sheet so that the side in contact with the contents became the coating layer. A three-piece can comprising the can body, the can lid, and the can bottom was manufactured.

【0027】実施例2 ポリエステルbをポリエステルcとしたほかは実施例1
と同様にして、3ピース缶を製造した。 実施例3 ポリエステルbをポリエステルdとしたほかは実施例1
と同様にして、3ピース缶を製造した。 実施例4 実施例3において、二軸延伸、熱固定後のフィルムを得
た後、フィルムを純水125℃中で1時間浸漬処理を施
した後、乾燥し使用する以外は実施例3と同様にして、
3ピース缶を製造した。
Example 2 Example 1 except that polyester b was changed to polyester c
A three-piece can was manufactured in the same manner as in. Example 3 Example 1 except that polyester b was changed to polyester d
A three-piece can was manufactured in the same manner as in. Example 4 The same as Example 3 except that the film after biaxial stretching and heat setting was obtained in Example 3 and then the film was immersed in pure water at 125 ° C. for 1 hour and then dried and used. And then
Three-piece cans were manufactured.

【0028】比較例1 ポリエステルbをポリエステルaとしたほかは実施例1
と同様にして、3ピース缶を製造した。 比較例2 ポリエステルbをポリエステルeとしたほかは実施例1
と同様にして、3ピース缶を製造した。以上、得られた
結果をまとめて下記表1に示す。
Comparative Example 1 Example 1 except that polyester b was changed to polyester a
A three-piece can was manufactured in the same manner as in. Comparative Example 2 Example 1 except that polyester b was changed to polyester e
A three-piece can was manufactured in the same manner as in. The results obtained above are summarized in Table 1 below.

【0029】[0029]

【表1】 [Table 1]

【0030】[0030]

【発明の効果】本発明の3ピース缶被覆用ポリエステル
フィルムは、水あるいは熱水による抽出成分が少なく、
衛生上優れており、その工業的価値は高い。
The polyester film for coating a three-piece can of the present invention has a small amount of water or hot water extractable components,
It is excellent in hygiene and its industrial value is high.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 接着剤で金属にラミネート被覆・製缶さ
れた後の末端カルボキシル基濃度が50当量/t未満で
あり、かつ、接着剤で金属にラミネート被覆・製缶され
た後に125℃の純水で1時間のレトルト処理によって
抽出される低分子量物が被覆表面1cm2 当たり2.0
μg以下であることを特徴とする3ピース缶被覆用ポリ
エステルフィルム。
1. The concentration of a terminal carboxyl group after being laminated and coated on a metal with an adhesive is less than 50 equivalents / t, and at 125 ° C. after being laminated and coated on a metal with an adhesive and produced. Low molecular weight substances extracted by pure water retort treatment for 1 hour are 2.0 per cm 2 of coated surface.
A polyester film for covering a three-piece can, which is characterized in that it is not more than μg.
JP22140493A 1993-09-06 1993-09-06 Polyester film for 3-piece can coating Expired - Fee Related JP3298712B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22140493A JP3298712B2 (en) 1993-09-06 1993-09-06 Polyester film for 3-piece can coating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22140493A JP3298712B2 (en) 1993-09-06 1993-09-06 Polyester film for 3-piece can coating

Publications (2)

Publication Number Publication Date
JPH0770341A true JPH0770341A (en) 1995-03-14
JP3298712B2 JP3298712B2 (en) 2002-07-08

Family

ID=16766224

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22140493A Expired - Fee Related JP3298712B2 (en) 1993-09-06 1993-09-06 Polyester film for 3-piece can coating

Country Status (1)

Country Link
JP (1) JP3298712B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09302113A (en) * 1996-05-16 1997-11-25 Toray Ind Inc Biaxially oriented polyester film for molding container
US6525165B1 (en) 1998-07-03 2003-02-25 Teijin Limited Trimethylene-2, 6-naphthalene dicarboxylate (co)polymer film, quaternary phosphonium sulfonate copolymer and compositions thereof
JP2004502601A (en) * 2000-07-03 2004-01-29 テトラ ラバル ホールデイングス エ フイナンス ソシエテ アノニム Packaging machines for continuous production of sealed packaging

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09302113A (en) * 1996-05-16 1997-11-25 Toray Ind Inc Biaxially oriented polyester film for molding container
US6525165B1 (en) 1998-07-03 2003-02-25 Teijin Limited Trimethylene-2, 6-naphthalene dicarboxylate (co)polymer film, quaternary phosphonium sulfonate copolymer and compositions thereof
JP2004502601A (en) * 2000-07-03 2004-01-29 テトラ ラバル ホールデイングス エ フイナンス ソシエテ アノニム Packaging machines for continuous production of sealed packaging

Also Published As

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