JPH06380B2 - Polyester multilayer container - Google Patents
Polyester multilayer containerInfo
- Publication number
- JPH06380B2 JPH06380B2 JP21224985A JP21224985A JPH06380B2 JP H06380 B2 JPH06380 B2 JP H06380B2 JP 21224985 A JP21224985 A JP 21224985A JP 21224985 A JP21224985 A JP 21224985A JP H06380 B2 JPH06380 B2 JP H06380B2
- Authority
- JP
- Japan
- Prior art keywords
- polyester
- layer
- inorganic particles
- container
- particle size
- 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.)
- Expired - Lifetime
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- Containers Having Bodies Formed In One Piece (AREA)
- Laminated Bodies (AREA)
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明はポリエステル多層容器に関する。詳しくは板状
不活性無機粒子を含有するポリエステルから成る層を少
なくともその一層として有する二軸配向ポリエステル多
層容器に関する。DETAILED DESCRIPTION OF THE INVENTION <Field of Industrial Application> The present invention relates to a polyester multilayer container. More specifically, the present invention relates to a biaxially oriented polyester multilayer container having at least one layer made of polyester containing plate-like inert inorganic particles.
<従来技術> ポリエステル特にテレフタル酸を主たる酸成分とするポ
リエステルは機械的性質や耐薬品性等にすぐれるため繊
維やフイルム用素材として汎用され、又最近ではガラス
にかわる容器としても注目されてきた。<Prior Art> Polyesters, particularly polyesters containing terephthalic acid as a main acid component, have been widely used as materials for fibers and films because of their excellent mechanical properties and chemical resistance, and have recently been attracting attention as containers for glass. .
しかし、ポリエステルを容器等の包装材料に用いた場合
ポリエチレンやポリプロピレン等よりはすぐれるがガラ
スや金属に比べた場合ガスバリア性が必ずしも充分でな
く、その改善が望まれている。However, when polyester is used as a packaging material for containers and the like, it is superior to polyethylene, polypropylene and the like, but the gas barrier property is not always sufficient as compared with glass and metal, and improvement thereof is desired.
ポリエステルのガスバリア性を改善する方法としてポリ
塩化ビニリデンをコーテイングする方法、ポリビニルア
ルコールを積層する方法、カフエイン、テオプロミン等
有機物をブレンドする方法(RD230,029),ポリエチ
レンイソフタレート等特殊ポリエステルをブレンド或い
は積層する方法(特開昭59−64658号公報,特開昭59−3
9547号公報),メタキシリレンジアミン−アジピン酸ポ
リアミド(MXD6ナイロン)をブレンド或いは積層す
る方法(特開昭58−160,344号公報,特開昭57−123,0
51号公報)等各種の方法が提案されている。しかし、ポ
リ塩化ビニリデンやMXD6ナイロンを使用する方法は
ハロゲンや窒素原子を含むため焼却時に有毒ガス発生の
問題があり、ポリビニルアルコールを使用する方法はポ
リビニルアルコールが熱的に弱いため溶融成形時やけが
起つたり、又水分の影響を受け易い。又、カフエイン等
を使用する方法は容器の充填物によつては溶出のおそれ
がある。ポリエチレンイソフタレートを使用する方法に
はかかる問題は存在しないが充分なバリア性を得るため
には多量にブレンド又は積層する必要があり、容器の物
性低下のおそれがある。As a method to improve the gas barrier property of polyester, a method of coating polyvinylidene chloride, a method of laminating polyvinyl alcohol, a method of blending organic substances such as caffeine and theopromine (RD230,029), and blending or laminating a special polyester such as polyethylene isophthalate Method (JP-A-59-64658, JP-A-59-3)
9547), and a method of blending or laminating metaxylylenediamine-adipic acid polyamide (MXD6 nylon) (JP-A-58-160,344, JP-A-57-123,0).
Various methods such as Japanese Patent No. 51) have been proposed. However, the method of using polyvinylidene chloride or MXD6 nylon has a problem of generating toxic gas when incinerated because it contains halogen or nitrogen atoms, and the method of using polyvinyl alcohol is injured during melt molding because polyvinyl alcohol is thermally weak. It is easy to get up and is affected by moisture. Further, the method using caffeine or the like may cause elution depending on the filling material of the container. The method using polyethylene isophthalate does not have such a problem, but in order to obtain a sufficient barrier property, it is necessary to blend or laminate a large amount, and there is a possibility that the physical properties of the container may deteriorate.
一方、ガラス繊維やタルク等の無機粒子を配合したポリ
エステルからなる容器が知られている。例えば特公昭55
−11136号公報ではガラスフレークスをクロムやシリカ
系処理剤で処理後0.1〜1重量%添加することが知ら
れている。しかし、この容器もガスバリア性は不充分な
ものでしかない。特開昭57−70154号公報で1〜10μ
の無機粒子を添加し、光透過率30〜80%にしてスリ
ガラス調にしたポリエステル容器は公知である。又、特
開昭58−20443号公報にはガラス粒体0.1〜30重量
%を内層以外に用い、高級ガラス調にしたポリエステル
容器の記載がある。これらはいずれも特殊な容器外観を
付与することを目的としたものでありガスバリア性に関
しては何も述べてない。又、特開昭57−73045号公報,5
8−20634号公報にはアスペクト比3以上のガラス繊維
を、特開昭58−20635号公報には肉厚より小さい粒径の
ガラス粒子を0.1〜30重量%配合したポリエステル
容器が記載されている。又、特開昭56−2342号公報,特
開昭56−21832号公報,特開昭56−21833号公報ではカオ
リン,タルク,ステアリン酸ナトリウム,安息香酸ナト
リウム等を0.002〜0.5重量%配合するものが開
示されている。更に、特開昭57−207639号公報では無機
粉末,有機酸塩等を配合するものが開示されている。こ
れらはいずれもポリエステルの結晶性を向上させ容器の
耐熱性,耐熱収縮性向上を目的としたものであつて、ガ
スバリア性に関する記載は一切ない。又、特開昭56−18
646号公報には二酸化珪素を配合するものが記載されて
いるがこれは低アルデヒド化を目的としたものである。
特開昭58−20636号公報には、厚み10μ以下、粒径1
0メツシユ以下の板状ガラス粉体を0.1〜30重量%
配合したポリエステル容器が開示されている。On the other hand, containers made of polyester containing inorganic particles such as glass fibers and talc are known. For example, Japanese Examined Shoko 55
No. 11136 discloses that glass flakes are treated with chromium or a silica-based treating agent and then added in an amount of 0.1 to 1% by weight. However, this container also has an insufficient gas barrier property. In JP-A-57-70154, 1 to 10 μm
A polyester container in which the inorganic particles of (1) are added to give a light transmittance of 30 to 80% and which has a ground glass appearance is known. Further, JP-A-58-20443 describes a high-grade glass-like polyester container using 0.1 to 30% by weight of glass granules other than the inner layer. All of these are intended to give a special container appearance, and nothing is said about gas barrier properties. In addition, JP-A-57-73045, 5
JP-A-8-20634 discloses a polyester container in which glass fibers having an aspect ratio of 3 or more are blended, and JP-A-58-20635 discloses a polyester container containing 0.1 to 30% by weight of glass particles having a particle diameter smaller than the wall thickness. ing. Further, in JP-A-56-2342, JP-A-56-21832 and JP-A-56-21833, kaolin, talc, sodium stearate, sodium benzoate, etc. are added in an amount of 0.002-0.5 weight. % Formulation is disclosed. Further, JP-A-57-207639 discloses a composition containing inorganic powder, organic acid salt and the like. All of these are intended to improve the crystallinity of polyester and improve the heat resistance and heat shrinkage resistance of the container, and there is no description regarding gas barrier properties. Also, JP-A-56-18
Japanese Patent No. 646 describes a composition containing silicon dioxide, which is intended to reduce aldehyde.
JP-A-58-20636 discloses that the thickness is 10 μm or less and the particle size is 1
0.1 to 30% by weight of plate-like glass powder of 0 mesh or less
A blended polyester container is disclosed.
本発明者らは、前述のような欠点を解決しうるガスバリ
ア性改良法を検討した結果、無機粒子のうち特定の形状
と大きさを有するものをポリエステルに配合すれば目的
を達することができることを見い出した。The present inventors have studied a gas barrier property improving method capable of solving the above-mentioned drawbacks, and as a result, it has been found that the objective can be achieved if inorganic particles having a specific shape and size are blended with polyester. I found it.
<発明の目的> 本発明は、ガスバリア性に優れた二軸配向ポリエステル
多層容器を提供することを目的とする。<Object of the Invention> An object of the present invention is to provide a biaxially oriented polyester multilayer container having excellent gas barrier properties.
<発明の構成> 本発明は平均粒径5μ以下の板状不活性無機粒子を0.
01〜30重量%含有するポリエステルから成る層を最
内層以外の少なくとも一層とし、該無機粒子を含有しな
いポリエステルから成る層を少なくとも最内層とする二
軸配向ポリエステル多層容器である。<Structure of the Invention> The present invention provides a plate-like inactive inorganic particle having an average particle size of 5 μm or less with an average particle size of 0.
A biaxially oriented polyester multi-layer container having at least one layer other than the innermost layer of a polyester containing 01 to 30% by weight and at least an innermost layer of a polyester not containing the inorganic particles.
本発明において「容器」とはボトル、缶等の中空容器を
いう。これらは押出成形、射出成形によつて面状又は管
状或いは有底中空状に成形され、更に圧縮成形,真空成
形,ブロー成形等によつて少なくとも一部を二軸に延伸
配向させることによつて得られる。これらは二層以上の
多層のうち最内層以外の少なくとも一層が前記板状不活
性無機粒子を配合されたポリエステル層からなるもので
ある。In the present invention, the “container” refers to a hollow container such as a bottle or a can. These are molded into a planar shape or tubular shape or hollow shape with a bottom by extrusion molding or injection molding, and at least a part of them are stretched and oriented biaxially by compression molding, vacuum molding, blow molding or the like. can get. Among these, at least one layer other than the innermost layer of the two or more layers is composed of a polyester layer containing the plate-like inert inorganic particles.
本発明において「ポリエステル」とは、芳香族ジカルボ
ン酸を主たる酸成分とし、脂肪族グリコールを主たるグ
リコール成分とするポリエステルであり、ポリエチレン
テレフタレート、ポリエチレン−2,6−ナフタレート
等結晶性芳香族ポリエステルを主たる対象とするが、テ
レフタル酸ナフタレン−2,6−ジカルボン酸等の一部
を例えばイソフタル酸,ナフタレン−2,7−ジカルボ
ン酸の如き芳香族ジカルボン酸,ヘキサヒドロテレフタ
ル酸,ヘキサヒドロイソフタル酸の如き脂環族ジカルボ
ン酸,アジピン酸,セバチン酸の如き脂肪族ジカルボン
酸,p−β−ヒドロキシエトキシ安息香酸、ε−オキシ
カブロン酸の如きオキシ酸等の他の二官能性カルボン酸
及び/又はエチレングリコールの一部を例えばジエチレ
ングリコール,トリメチレングリコール,テトラメチレ
ングリコール,ヘキサメチレングリコール,ネオペンチ
ルグリコール,1,1−シクロヘキサンジメチロール,
1,4−シクロヘキサンジメチロールの如き他のグリコ
ールで置換したポリエステルであつても良い。またペン
タエリスリトール,トリメリツト酸,トリメシン酸等又
はそのエステル形成性誘導体の如き多官能化合物の一種
以上及び/又はo−ベンゾイル安息香酸等の単官能化合
物の一種以上を共重合せしめたものであつてもよい。更
に、必要に応じて任意の添加剤,例えば着色剤,螢光増
白剤,安定剤,紫外線吸収剤,エーテル結合防止剤,難
燃化剤,帯電防止剤等を使用しても良い。In the present invention, the "polyester" is a polyester having an aromatic dicarboxylic acid as a main acid component and an aliphatic glycol as a main glycol component, and mainly a crystalline aromatic polyester such as polyethylene terephthalate or polyethylene-2,6-naphthalate. As a target, a part of terephthalic acid naphthalene-2,6-dicarboxylic acid or the like is partially substituted with aromatic dicarboxylic acid such as isophthalic acid, naphthalene-2,7-dicarboxylic acid, hexahydroterephthalic acid or hexahydroisophthalic acid. Aliphatic dicarboxylic acids, aliphatic dicarboxylic acids such as adipic acid, sebacic acid, p-β-hydroxyethoxybenzoic acid, other difunctional carboxylic acids such as oxyacids such as ε-oxycabroic acid, and / or ethylene glycol Part of, for example, diethylene glycol, tri Methylene glycol, tetramethylene glycol, hexamethylene glycol, neopentyl glycol, 1,1-cyclohexanedimethylol,
It may be a polyester substituted with other glycols such as 1,4-cyclohexanedimethylol. In addition, one or more polyfunctional compounds such as pentaerythritol, trimellitic acid, trimesic acid and the like or ester-forming derivatives thereof and / or one or more monofunctional compounds such as o-benzoylbenzoic acid may be copolymerized. Good. Further, if desired, any additive such as a colorant, a fluorescent whitening agent, a stabilizer, a UV absorber, an ether bond inhibitor, a flame retardant, an antistatic agent, etc. may be used.
本発明で最内層以外の少なくとも一層に配合する不活性
無機粒子は板状である必要がある。粒状(球状,楕円体
状,紡錐体状,四面体状等々),棒状(針状,星状,棒
状,管状,糸状,短冊状等),無定形,塊状状等では本
発明の目的に適合しない。板状であるならば、形態が円
形であつても小判形でもその他三角,四角,菱形,短
形,六角,八角形等いずれであつてもよい。これらの板
状不活性無機粒子の具体的な例としては下記のものが例
示される。カオリン族、例えばデイツカイト,ナクライ
ト,カオリナイト,アノーキサイト;ハロイサイトのう
ち板状のもの;蛇紋石族,例えばリザルダイト,6−層
蛇紋石,アンチゴライト;モンモリロナイト鉱物,例え
ばモンモリロナイト,ザウコナイト,ノントロナイト,
サボナイト,ヘクトライト;バーミキユライト鉱物,例
えばバーミキユライト;雲母鉱物,例えばイライト,セ
リサイト,海緑石;機械的粉砕(ジヨークラツシヤー,
スタンプミル,ボールミル,カツターミル,エツデイミ
ル,マイクロナイザー等)によるAl,Cu,Fe,P
b,Sn,Fe合金;水溶液電解法によるAg,Co,
Cu,Fe,Ni,Sb,Sn等のうち板状のもの;M
g微粒子;Al2O3,Al2O3水和物,Fe
2O3,ZnO,Cr2O3,PbO,Co(O
H)2,Pb(OH)4,CaWO3,CaCu4Cl
O,AgBr,AgI,BaSO4,PbI2,MgC
O3(塩基性),BaSO4等合成粉体粒子等々。これ
らのうちでカオリン族,蛇紋石族,モンモリロナイト鉱
物,バーミキユライト鉱物,および雲母鉱物が好ましく
特にカオリナイト、デイツカイト,バーミキユライト,
モンモリロナイトおよびセリサイトが好ましい。The inert inorganic particles to be blended in at least one layer other than the innermost layer in the present invention need to be plate-shaped. Granular (spherical, ellipsoidal, spindle-shaped, tetrahedral, etc.), rod-shaped (needle-shaped, star-shaped, rod-shaped, tubular, thread-shaped, strip-shaped, etc.), amorphous, lump-shaped, etc. not compatible. If it has a plate shape, it may have a circular shape, an oval shape, or a triangular shape, a square shape, a rhombus shape, a short shape, a hexagonal shape, an octagonal shape, or the like. The following are illustrated as specific examples of these plate-like inert inorganic particles. Kaolins such as ditzkite, nacrite, kaolinite, anoxite; plates of halloysite; serpentine family such as risaldite, 6-layer serpentine, antigorite; montmorillonite minerals such as montmorillonite, sauconite, nontroite Knight,
Savonite, hectorite; vermiculite minerals, such as vermiculite; mica minerals, such as illite, sericite, glauconite; mechanical grinding (Jiyokratsiya,
Stamp mill, ball mill, cutter mill, eddy mill, micronizer, etc.) Al, Cu, Fe, P
b, Sn, Fe alloy; Ag, Co, by aqueous solution electrolysis method
Plate-shaped one of Cu, Fe, Ni, Sb, Sn, etc .; M
g Fine particles; Al 2 O 3 , Al 2 O 3 hydrate, Fe
2 O 3 , ZnO, Cr 2 O 3 , PbO, Co (O
H) 2 , Pb (OH) 4 , CaWO 3 , CaCu 4 Cl
O, AgBr, AgI, BaSO 4 , PbI 2 , MgC
O 3 (basic), synthetic powder particles such as BaSO 4, etc. Among these, kaolin group, serpentine group, montmorillonite mineral, vermiculite mineral, and mica mineral are preferable, and kaolinite, dateskite, vermiculite,
Montmorillonite and sericite are preferred.
板状の不活性無機粒子は平均粒径が5μ以下であること
が必要である。5μ以上であると成形品の表面平坦性が
低下する。好ましくは2μ以下、特に好ましくは1μ以
下である。ここで平均粒径とは、測定した全粒子の50
重量%の点にある粒子の「等価球形直径」を意味する。
「等価球直径」とは粒子と同じ容積を有する想像上の球
の直径を意味し、粒子の電子顕微鏡写真または通常の沈
降法による測定から計算することが出来る。The plate-like inert inorganic particles need to have an average particle size of 5 μm or less. If it is 5 μm or more, the surface flatness of the molded product is deteriorated. It is preferably 2 μm or less, particularly preferably 1 μm or less. Here, the average particle size is 50 of all measured particles.
It means the "equivalent spherical diameter" of a particle in% by weight.
By "equivalent sphere diameter" is meant the diameter of an imaginary sphere having the same volume as the particle, which can be calculated from electron micrographs of the particle or measurements by conventional sedimentation methods.
この平均粒径5μ以下の不活性無機粒子の粒度分布につ
いては、約10μ以上の粗大粒子をほとんど含まず、微
細側にシヤープな分布をもつものほど好ましい。With respect to the particle size distribution of the inert inorganic particles having an average particle size of 5 μm or less, it is more preferable that almost no coarse particles having a particle size of about 10 μm or more are contained and a fine distribution has a sharp distribution.
本発明ではこの板状不活性無機粒子を含むポリエステル
層における該不活性無機粒子の含有量は0.01〜30
重量%,好ましくは0.02〜10重量%である。容器
全体に対しては0.005〜15重量%,好ましくは0.0
1〜5重量%である。無機粒子の含有量が下限未満では
ガスバリア性向上効果は小さく、又上限を超えるとガス
バリア性の効果が飽和するばかりでなくボトル強度が低
下する。透明性を得るには全体に対して0.3重量%以
下に抑える。In the present invention, the content of the inert inorganic particles in the polyester layer containing the plate-like inert inorganic particles is 0.01 to 30.
%, Preferably 0.02 to 10% by weight. 0.005 to 15% by weight, preferably 0.0
It is 1 to 5% by weight. If the content of the inorganic particles is less than the lower limit, the effect of improving the gas barrier property is small, and if it exceeds the upper limit, not only the effect of the gas barrier property is saturated, but also the bottle strength decreases. To obtain transparency, the content is controlled to 0.3% by weight or less based on the whole.
本発明において板状不活性無機粒子のポリエステルへの
配分方法はポリエステル重合の中期以前が好ましく、特
にエステル化又はエステル交換中期(内温160〜20
0℃近辺)が好ましい。これは添加時に無機粒子の凝集
を防ぐ上から重要なことである。しかし、エステル化又
はエステル交換中期以降、重合中期以前でも無機粒子ス
ラリーを100〜200℃に加熱して添加すれば十分に
目的を達することが出来る。重合中期以降の添加、或い
はポリエステルの重合完了後成形前にチツプに直接ブレ
ンドする方法はボイドがはいり易く、透明性を得ること
は困難であるが目的を達成することはできる。In the present invention, the method for distributing the plate-like inert inorganic particles to the polyester is preferably before the middle stage of polyester polymerization, and particularly in the middle stage of esterification or transesterification (internal temperature of 160 to 20).
(Around 0 ° C.) is preferable. This is important from the viewpoint of preventing aggregation of inorganic particles during addition. However, even after the middle stage of esterification or transesterification and before the middle stage of polymerization, heating the inorganic particle slurry to 100 to 200 [deg.] C. and adding it can sufficiently achieve the purpose. The method of adding after the middle stage of the polymerization or directly blending with the chip after the completion of the polymerization of the polyester and before the molding is easy to introduce voids, and it is difficult to obtain transparency, but the object can be achieved.
ポリエステル製造工程への無機粒子の添加方法としては
0.5〜20重量%のグリコールスラリーとして添加す
る方法が良い。ポリエステルに無機粒子を高濃度で上記
の方法で添加、重合してこれをマスターバツチとし別途
製造した無機粒子を含まないポリエステルで所望の粒子
量になる様に希釈することもできる。As a method of adding the inorganic particles to the polyester production process, a method of adding as a glycol slurry of 0.5 to 20% by weight is preferable. Inorganic particles may be added to polyester at a high concentration by the above-mentioned method, polymerized, and this may be used as a master batch to be diluted with a separately produced polyester containing no inorganic particles so as to obtain a desired particle amount.
本発明において板状無機粒子を含む層が最内層にあると
内容物を充填した時に一部が溶解、抽出される恐れがな
いとは言えず食品衛生上好ましくないので該無機粒子を
含むポリエステル層の最内層としての使用は避けるべき
である。従つて最内層は無機粒子を含まないポリエステ
ルからなる層である。この板状無機粒子を含まないポリ
エステルからなる層で無機粒子含有ポリエステルから成
る層を挟んだ三層構造でもよく、それ以上の多層でもよ
い。同じポリエステルから成る多層から構成されている
ので層間の接着性はよく層間剥離の心配がない。In the present invention, the layer containing the plate-shaped inorganic particles is the innermost layer, and when the contents are filled, it cannot be said that there is no risk that it will be partially dissolved and extracted. Use as the innermost layer of should be avoided. Therefore, the innermost layer is a layer made of polyester containing no inorganic particles. A three-layer structure in which a layer made of polyester containing no inorganic particles is sandwiched between layers made of polyester containing inorganic particles, or a multilayer having more layers may be used. Since it is composed of multiple layers made of the same polyester, the adhesion between layers is good and there is no risk of delamination.
多層容器は、多層射出や多層押し出しでまずプリフオー
ム又はパイプ,シート等に成形し、次いでこれをポリエ
ステルの二次転移温度以上融点以下に加熱して(場合に
より有底化後)、二軸配向ブローや金型内で圧延、真空
成形による深絞り等によつて二軸配向容器とする。A multilayer container is first formed into a preform, pipe, sheet, etc. by multilayer injection or extrusion, and then heated to a temperature above the second-order transition temperature of polyester and below the melting point (after bottoming in some cases), and then biaxially oriented blow. A biaxially oriented container is obtained by rolling in a metal mold or deep drawing by vacuum forming.
<発明の効果> 本発明の多層容器は無機粒子を含まないポリエステル容
器に比べガスバリア性が10%以上高い特徴を有し、炭
酸飲料やビール容器等ガスバリア性を要求される容器と
して充分使用しうる。<Effects of the Invention> The multi-layer container of the present invention has a characteristic that the gas barrier property is 10% or more higher than that of a polyester container containing no inorganic particles, and can be sufficiently used as a container such as a carbonated beverage or a beer container which is required to have a gas barrier property. .
<実施例> 以下実施例によつて本発明を具体的に説明する。実施例
中「部」は全て重量部を表わし、又各項目は下記測定法
によつた。<Examples> The present invention will be specifically described with reference to Examples below. All "parts" in the examples represent parts by weight, and each item was measured by the following measuring methods.
○固有粘度〔η〕: ポリマーのオルソクロロフエノール溶液の35℃におけ
る溶液粘度から算出した。O Intrinsic viscosity [η]: Calculated from the solution viscosity of the polymer orthochlorophenol solution at 35 ° C.
○不活性固体微粒子の平均粒径: 島津製作所製CP−50型Centrifugal Particle Size An
alyserを用いて測定した。得られた遠心沈降曲線を基に
算出した各粒径の粒子とその存在量とのcumulative曲線
から、50mass percent に相当する粒径を読み取り、
この値を上記平均粒径とした(Book「粒度測定技術」日
刊工業新聞社発行、1975年,頁242〜247参
照)。○ Average particle size of inert solid fine particles: CP-50 type Centrifugal Particle Size An manufactured by Shimadzu Corporation
It was measured using an alyser. The particle size corresponding to 50 mass percent is read from the cumulative curve of the particles of each particle size and their abundance calculated based on the obtained centrifugal sedimentation curve,
This value was defined as the average particle size (see Book "Particle Size Measurement Technology", Nikkan Kogyo Shimbun, 1975, pages 242 to 247).
○ガスバリア性: 成形品から30mmφのサンプルを切り出しこれを理化精
機工業(株)製気体透過率測定装置K−315N−03を用
い、30℃にてCO2ガスの透過係数を測定した。Gas barrier property: A 30 mmφ sample was cut out from the molded product, and the permeability coefficient of CO 2 gas was measured at 30 ° C. using a gas permeability measuring device K-315N-03 manufactured by Rika Seiki Co., Ltd.
実施例1〜9,比較例1〜7 テレフタル酸ジメチル100部,エチレングリコール7
0部,酢酸マンガン四水塩0.03部を反応機に入れ1
40〜240℃でエステル交換反応を行なつた。Examples 1 to 9, Comparative Examples 1 to 7 100 parts of dimethyl terephthalate, ethylene glycol 7
1 part of 0 parts and 0.03 parts of manganese acetate tetrahydrate were put into the reactor.
The transesterification reaction was carried out at 40 to 240 ° C.
他方、平均粒径0.7μのカオリナイトをエチレングリ
コール中に入れホモグナザー,サンドグラインダー,デ
カンター処理して平均粒径0.65μのカオリナイト1
0wt%エチレングリコールスラリーを作成した。On the other hand, kaolinite with an average particle size of 0.7μ was put in ethylene glycol and treated with a homogenizer, a sand grinder and a decanter to obtain kaolinite with an average particle size of 0.65μ.
A 0 wt% ethylene glycol slurry was prepared.
前記エステル交換反応中、内温が170℃になつた時点
でこのエチレングリコールスラリーを、カオリナイトが
第1表の添加量になる様に添加した。更に反応を進め、
エステル交換反応の終了した時点で正リン酸0.015
部,二酸化ゲルマニウム0.012部を添加し重縮合反
応を行なつて固有粘度0.65のポリエステルを得た。
更にこれを200℃不活性気流中固相重合を行ない最終
的に固有粘度0.75のポリマー(A)を得た。他方、同
じ様にしてカオリナイトを含有しないポリマーBを得
た。During the transesterification reaction, when the internal temperature reached 170 ° C., this ethylene glycol slurry was added so that the amount of kaolinite added was as shown in Table 1. Further reaction,
Orthophosphoric acid 0.015 at the end of transesterification
And 0.012 parts of germanium dioxide were added and polycondensation reaction was carried out to obtain a polyester having an intrinsic viscosity of 0.65.
Further, this was subjected to solid phase polymerization in an inert gas stream at 200 ° C. to finally obtain a polymer (A) having an intrinsic viscosity of 0.75. On the other hand, Kaolinite-free polymer B was obtained in the same manner.
両ポリマーを乾燥後、シリンダー温度280℃の射出成
形機を用いてAを中間層,Bを内,外層(内層:中間
層:外層=3:4:3)とする重量49g,長さ176
mm,肉厚3.5mmの円筒状有底パリソンを成形した。こ
の時プリフオーム金型は冷水により10℃に冷却した。
次いで該パクソンを内部温度が90〜105℃となる様
に再加熱した後、二軸延伸ブローを行ない高さ270m
m,胴部の径80〜90mm及び胴部の平均肉厚が0.3
5mmの内容積1のボトルを得た。(胴部の面積延伸倍
率10倍)このボトルの諸物性を第1表に示した。After drying both polymers, using an injection molding machine at a cylinder temperature of 280 ° C., A is an intermediate layer and B is an inner layer and an outer layer (inner layer: intermediate layer: outer layer = 3: 4: 3), weight 49 g, length 176.
A cylindrical bottomed parison with a thickness of 3.5 mm and a thickness of 3.5 mm was molded. At this time, the preform mold was cooled to 10 ° C. with cold water.
Then, the Paxson was reheated to an internal temperature of 90 to 105 ° C. and then biaxially stretched and blown to a height of 270 m.
m, the diameter of the body is 80 to 90 mm, and the average thickness of the body is 0.3
A bottle with an internal volume of 1 of 5 mm was obtained. (Area draw ratio of body: 10 times) Table 1 shows the physical properties of this bottle.
なお、実施例5常温のカオリナイトのエチレングリコー
ルスラリーをエステル交換末期(内温240℃)に添加し
たもの。Example 5 An ethylene glycol slurry of kaolinite at room temperature was added at the final stage of transesterification (internal temperature: 240 ° C).
実施例6は添加時期は実施例5と同じであるがカオリナ
イトのエチレングリコールスラリーを150℃に加熱し
て添加したものである。In Example 6, the addition time is the same as in Example 5, but an ethylene glycol slurry of kaolinite is heated to 150 ° C. and added.
又、実施例7はポリマーの製造時、カオリナイトの添加
量を15重量%とし、マスターバツチとし、これをボト
ル成形前無添加のポリエチレンテレフタレートで10倍
に希釈ブレンドし成形したものである。Further, in Example 7, during the production of the polymer, the amount of kaolinite added was 15% by weight to prepare a master batch, which was molded by diluting and blending it 10 times with polyethylene terephthalate without additives before bottle molding.
実施例8は無添加のポリエチレンテレフタレートにカオ
リナイトを未処理のまま粉体で1.5wt%タンブラー中
でブレンドし成形したものである。In Example 8, additive-free polyethylene terephthalate was blended with kaolinite as a powder in an untreated state in a tumbler of 1.5 wt% and molded.
実施例9以降はカオリナイト以外の無機粒子を実施例3
と同じ様に処理、添加し、ポリマーとし、更にボトルに
成形したものである。In Example 9 and later, inorganic particles other than kaolinite were used in Example 3
It is treated and added in the same manner as above, made into a polymer, and further molded into a bottle.
実施例12,比較例5 実施例3のポリマーA及びポリマーBを用い、シリンダ
ー温度280℃の共押出機を用いてA層/B層1/1の
300μのフイルムを共押し出した。このフイルムを9
0℃に加熱しB層が内側になる様カツプ状金型中で圧縮
成形し、口径100mmφ,底部50mmφ,高さ50mmの
カツプを成形した。この成形品の胴部のCO2透過係数
は14cm3・cm/cm2・sec・cmHgであつた。 Example 12, Comparative Example 5 Polymer A and polymer B of Example 3 were used to coextrude a 300 μ film of A layer / B layer 1/1 with a coextruder having a cylinder temperature of 280 ° C. 9 of this film
It was heated to 0 ° C. and compression-molded in a cup-shaped mold so that the layer B was on the inside, to form a cup having a diameter of 100 mmφ, a bottom portion of 50 mmφ, and a height of 50 mm. The CO 2 permeation coefficient of the body of this molded product was 14 cm 3 · cm / cm 2 · sec · cmHg.
しかし、ポリマーBのみからなる同形のカツプのCO2
透過係数は16cm3・cm/cm2・sec・cmHgであつた。However, the same shape of CO 2 consisting of polymer B alone
The transmission coefficient was 16 cm 3 · cm / cm 2 · sec · cmHg.
Claims (2)
0.01〜30重量%含有するポリエステルから成る層を最
内層以外の少なくとも一層とし、該無機粒子を含有しな
いポリエステルから成る層を少なくとも最内層とする二
軸配向ポリエステル多層容器。1. A plate-like inert inorganic particle having an average particle size of 5 μm or less
A biaxially oriented polyester multi-layer container in which a layer made of polyester containing 0.01 to 30% by weight is at least one layer other than the innermost layer and a layer made of polyester not containing the inorganic particles is at least the innermost layer.
族、モンモリロナイト鉱物,バーミキュライト鉱物およ
び雲母鉱物から選ばれる特許請求の範囲第1項記載の二
軸配向ポリエステル多層容器。2. The biaxially oriented polyester multilayer container according to claim 1, wherein the plate-like inert inorganic particles are selected from the group consisting of kaolin group, serpentine group, montmorillonite mineral, vermiculite mineral and mica mineral.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21224985A JPH06380B2 (en) | 1985-09-27 | 1985-09-27 | Polyester multilayer container |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21224985A JPH06380B2 (en) | 1985-09-27 | 1985-09-27 | Polyester multilayer container |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6273943A JPS6273943A (en) | 1987-04-04 |
| JPH06380B2 true JPH06380B2 (en) | 1994-01-05 |
Family
ID=16619440
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21224985A Expired - Lifetime JPH06380B2 (en) | 1985-09-27 | 1985-09-27 | Polyester multilayer container |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06380B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB9102374D0 (en) * | 1991-02-04 | 1991-03-20 | Ici Plc | Polymeric film |
| US6084019A (en) * | 1996-12-31 | 2000-07-04 | Eastman Chemical Corporation | High I.V. polyester compositions containing platelet particles |
| US8124202B2 (en) * | 2006-09-15 | 2012-02-28 | The Coca-Cola Company | Multilayer container for enhanced gas barrier properties |
-
1985
- 1985-09-27 JP JP21224985A patent/JPH06380B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6273943A (en) | 1987-04-04 |
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| EXPY | Cancellation because of completion of term |