JPH0952327A - Multilayer sheet and packaging container made of the same - Google Patents
Multilayer sheet and packaging container made of the sameInfo
- Publication number
- JPH0952327A JPH0952327A JP7227457A JP22745795A JPH0952327A JP H0952327 A JPH0952327 A JP H0952327A JP 7227457 A JP7227457 A JP 7227457A JP 22745795 A JP22745795 A JP 22745795A JP H0952327 A JPH0952327 A JP H0952327A
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- polypropylene
- packaging container
- resin composition
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000004806 packaging method and process Methods 0.000 title claims abstract description 15
- -1 polyethylene terephthalate Polymers 0.000 claims abstract description 41
- 229920000139 polyethylene terephthalate Polymers 0.000 claims abstract description 19
- 239000005020 polyethylene terephthalate Substances 0.000 claims abstract description 19
- 239000011342 resin composition Substances 0.000 claims abstract description 19
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims abstract description 8
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims abstract description 8
- 239000004743 Polypropylene Substances 0.000 claims description 35
- 229920001155 polypropylene Polymers 0.000 claims description 35
- 229920005989 resin Polymers 0.000 claims description 20
- 239000011347 resin Substances 0.000 claims description 20
- 239000000470 constituent Substances 0.000 claims description 12
- 230000006866 deterioration Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 9
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 8
- 238000011156 evaluation Methods 0.000 description 7
- 238000003856 thermoforming Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 239000000155 melt Substances 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000005336 cracking Methods 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 1
- YIMQCDZDWXUDCA-UHFFFAOYSA-N [4-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1CCC(CO)CC1 YIMQCDZDWXUDCA-UHFFFAOYSA-N 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000012685 gas phase polymerization Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 238000009863 impact test Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002762 monocarboxylic acid derivatives Chemical class 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Wrappers (AREA)
- Laminated Bodies (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は多層構造シート及び
それからなる包装容器に関する。更に詳しくは透明で成
形性に優れ、かつ耐衝撃性の経時的低下が少ない多層構
造シート及びそれからなる包装容器に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a multilayer structure sheet and a packaging container made of the same. More specifically, the present invention relates to a multi-layered sheet which is transparent and has excellent moldability and whose impact resistance is less likely to deteriorate over time, and a packaging container made of the same.
【0002】[0002]
【従来の技術】ポリエステル、特にポリエチレンテレフ
タレート(以下PETと記す)は、機械的特性、耐熱
性、耐薬品性、寸法安定性等が優れているために繊維、
フィルム、プラスチックとして広く利用されている。最
近、PETを原料とするシート及びそれからなる成形品
は容易に成形可能でかつ良好な透明性、光沢、ガス透過
性を有するため、種々の商品包装のための容器として利
用する試みがなされている。2. Description of the Related Art Polyesters, especially polyethylene terephthalate (hereinafter referred to as PET), are excellent in mechanical properties, heat resistance, chemical resistance, dimensional stability and the like.
Widely used as film and plastic. Recently, a sheet made of PET and a molded product made of PET are easily moldable and have good transparency, gloss, and gas permeability, so that attempts have been made to use them as containers for packaging various products. .
【0003】しかしながら、これらの包装容器は経時的
な物性の低下が起こり、この点を改善することが必要で
ある。前記のPETを原料とするシート及びそれからな
る包装容器は、多湿度雰囲気中で長時間放置すると耐衝
撃性が著しく低下する。通常の保管条件(30℃、50
%RH)においても、3か月以上経過すると耐衝撃性が
低下して割れやすくなるという欠点を有しておりその改
善が望まれていた。However, the physical properties of these packaging containers deteriorate with time, and it is necessary to improve this point. The impact resistance of the above-mentioned sheet made of PET as a raw material and the packaging container made of the PET is remarkably deteriorated when left for a long time in a high humidity atmosphere. Normal storage conditions (30 ℃, 50
% RH) also has a drawback that the impact resistance is lowered and cracking easily occurs after 3 months or more, and its improvement has been desired.
【0004】一方、ポリプロピレンは安価で柔軟性、衛
生適合性、耐水蒸気透過性に優れる等の特徴を有するこ
とから、中空成形品等の包装材料に広く使用されてい
る。しかしながら、ポリプロピレンを原料とするシート
及びそれからなる成形品は透明性が低いことや剛性に乏
しく熱成形時にドローダウンを起こしやすいなどの問題
点がある。On the other hand, polypropylene is widely used as a packaging material for hollow molded articles and the like because it is inexpensive and has characteristics such as flexibility, hygienic compatibility, and excellent water vapor permeation resistance. However, there are problems that the sheet made of polypropylene as a raw material and a molded product made of the same have low transparency and poor rigidity, and easily cause drawdown during thermoforming.
【0005】ポリプロピレンを原料とするシートの透明
性を改善する方法として、シンジオタクチック構造を有
するポリプロピレンを含むポリプロピレン樹脂組成物を
使用することが提案されている(特開平7−12645
4号公報、特開平7−126458号公報)。しかしな
がら、透明性は改善されるもののポリプロピレンを原料
とするシートのもう一つの課題である剛性の改善はなさ
れていない。As a method for improving the transparency of a sheet made of polypropylene as a raw material, it has been proposed to use a polypropylene resin composition containing polypropylene having a syndiotactic structure (Japanese Patent Laid-Open No. 7-12645).
No. 4, JP-A-7-126458). However, although the transparency is improved, the rigidity, which is another problem of the sheet made of polypropylene, has not been improved.
【0006】[0006]
【発明が解決しようとする課題】従って、本発明の目的
とするところは前記のPETを原料とするシートおよび
ポリプロピレンを原料とするシートの欠点をなくし、耐
衝撃性の経時的低下が少なく、かつ製膜性、透明性、包
装容器への二次加工性に優れるシートを提供することに
ある。Therefore, the object of the present invention is to eliminate the drawbacks of the sheet made of PET and the sheet made of polypropylene as described above, and the impact resistance is less deteriorated with time. An object of the present invention is to provide a sheet having excellent film formability, transparency, and secondary processability into a packaging container.
【0007】[0007]
【課題を解決するための手段】本発明者らはかかる目的
で鋭意研究を重ねた結果、PET層と特定のポリプロピ
レン樹脂組成物層からなる多層構造シートにおいて、P
ET層と特定のポリプロピレン樹脂組成物層との重量比
率を規定することによって、耐衝撃性の経時的低下が少
なく、透明性、製膜性、二次加工性および外観に優れた
多層構造シートが得られることを見出し本発明に到達し
たものである。Means for Solving the Problems As a result of intensive studies conducted by the present inventors for such a purpose, in a multilayer structure sheet comprising a PET layer and a specific polypropylene resin composition layer, P
By defining the weight ratio of the ET layer and the specific polypropylene resin composition layer, a multilayer structure sheet having less deterioration in impact resistance over time and excellent in transparency, film-forming property, secondary processability and appearance can be obtained. The present invention has been found to be obtained and has reached the present invention.
【0008】すなわち、本発明はシンジオタクチック構
造を有するポリプロピレンを含有するプロピレン樹脂組
成物からなる主構成層の両側に極限粘度が0.6〜1.
0dl/gのポリエチレンテレフタレート樹脂からなる補
助層を有する多層構造シートであって、主構成層と補助
層の重量比率が90:10〜40:60の範囲にあるこ
とを特徴とする多層構造シート及びそれからなる包装容
器に関するものである。That is, according to the present invention, the intrinsic viscosity is 0.6 to 1.2 on both sides of the main constituent layer made of a propylene resin composition containing polypropylene having a syndiotactic structure.
A multilayer structure sheet having an auxiliary layer of 0 dl / g polyethylene terephthalate resin, wherein the weight ratio of the main constituent layer and the auxiliary layer is in the range of 90:10 to 40:60, and It relates to a packaging container made of it.
【0009】[0009]
【発明の実施の形態】本発明で用いられるシンジオタク
チックポリプロピレンは、プロピレンモノマーからスリ
ラー重合法、塊状重合法、気相重合法等の公知の重合方
法により得られた13C−NMRによって測定されるシン
ジオタクチックペンタッド分率が0.7以上のポリプロ
ピレンであるが、本発明の多層構造シートの透明性およ
び機械物性を損なわないかぎり、プロピレン以外のコモ
ノマーを少量含有する共重合体であっても良い。BEST MODE FOR CARRYING OUT THE INVENTION The syndiotactic polypropylene used in the present invention is measured by 13 C-NMR obtained from a propylene monomer by a known polymerization method such as a thriller polymerization method, a bulk polymerization method and a gas phase polymerization method. A polypropylene having a syndiotactic pentad fraction of 0.7 or more, which is a copolymer containing a small amount of a comonomer other than propylene as long as the transparency and mechanical properties of the multilayer structure sheet of the present invention are not impaired. Is also good.
【0010】本発明に用いられるシンジオタクチック構
造を有するポリプロピレンを含有するプロピレン樹脂組
成物は、シンジオタクチックポリプロピレン5〜95重
量部、およびアイソタクチックポリプロピレン95〜5
重量部からなるポリプロピレン樹脂組成物であること
が、最も透明性に優れたシートを得られることから好ま
しい。シンジオタクチックポリプロピレンの割合が95
重量部を超えると、樹脂の流動性が悪くなり、シート製
膜が困難となる。また逆にアイソタクチックポリプロピ
レンの割合が95重量部を超えると、得られるシートの
透明性が不足してくる。The propylene resin composition containing the polypropylene having the syndiotactic structure used in the present invention comprises 5 to 95 parts by weight of syndiotactic polypropylene and 95 to 5 of isotactic polypropylene.
A polypropylene resin composition composed of parts by weight is preferable because a sheet having the highest transparency can be obtained. The ratio of syndiotactic polypropylene is 95
If it exceeds the weight part, the fluidity of the resin deteriorates and it becomes difficult to form a sheet. On the other hand, if the proportion of isotactic polypropylene exceeds 95 parts by weight, the transparency of the obtained sheet will be insufficient.
【0011】本発明に用いられるシンジオタクチック構
造を有するポリプロピレンを含有するプロピレン樹脂組
成物を得るための方法としては、任意の方法を採用し得
るがシンジオタクチックポリプロピレン樹脂とアイソタ
クチックポリプロピレン樹脂を、二軸混練機等を用いて
あらかじめ溶融下、混練しペレット化するのが好まし
い。As a method for obtaining a propylene resin composition containing polypropylene having a syndiotactic structure used in the present invention, any method can be adopted, but a syndiotactic polypropylene resin and an isotactic polypropylene resin are used. It is preferable to knead and pelletize under a molten condition in advance using a twin-screw kneader or the like.
【0012】本発明で用いられるポリプロピレン樹脂組
成物は、230℃におけるメルトフローレイトが0.1
〜10g/10min 、好ましくは0.5〜5g/10mi
n でる。230℃におけるメルトフローレイトが10.
0g/10min より高い場合は得られるシートの機械物
性が著しく低下し、耐衝撃性の十分な向上が見られな
い。また、230℃におけるメルトフローレイトが0.
1g/10min より低い場合は、樹脂流動性が悪くなり
シート製膜が困難となる。The polypropylene resin composition used in the present invention has a melt flow rate of 0.1 at 230 ° C.
-10g / 10min, preferably 0.5-5g / 10mi
n. Melt flow rate at 230 ° C is 10.
When it is higher than 0 g / 10 min, the mechanical properties of the obtained sheet are remarkably deteriorated and the impact resistance is not sufficiently improved. Further, the melt flow rate at 230 ° C. is 0.
If it is lower than 1 g / 10 min, the resin fluidity is deteriorated and it becomes difficult to form a sheet.
【0013】本発明で述べるポリプロピレン樹脂組成物
のメルトフローレイトとは、ポリプロピレン樹脂組成物
を、内径9.55mm、長さ162mmのシリンダーに充填
し、シリンダー内の樹脂を230℃で溶融したものに、
重さ2160g、直径9.4mmのプランジャーを載せて
均等に荷重をかけたときに、シリンダーの中央に設けた
径2.1mmのオリフィスより押し出される溶融重合体の
重量速度(g/10min )を測定した値を表す。The melt flow rate of the polypropylene resin composition described in the present invention means that the polypropylene resin composition is filled in a cylinder having an inner diameter of 9.55 mm and a length of 162 mm, and the resin in the cylinder is melted at 230 ° C. ,
When a plunger with a weight of 2160 g and a diameter of 9.4 mm was placed and the load was evenly applied, the weight velocity (g / 10 min) of the molten polymer extruded from the 2.1 mm diameter orifice provided in the center of the cylinder was measured. Indicates the measured value.
【0014】本発明に用いられるPET樹脂は、テレフ
タル酸またはそのエステル形成性誘導体(例えば低級ア
ルキルエステル等)と、エチレングリコール又はそのエ
ステル形成性誘導体(例えばモノカルボン酸エステルエ
チレンオキサイド等)とを公知の方法によって重縮合せ
しめて得られるものであり、PET樹脂本来の特性を損
なわない範囲で他の共重合成分を含んでいても良い。As the PET resin used in the present invention, terephthalic acid or its ester-forming derivative (for example, lower alkyl ester) and ethylene glycol or its ester-forming derivative (for example, monocarboxylic acid ester ethylene oxide) are known. It can be obtained by polycondensation by the above method, and may contain other copolymerization components as long as the original characteristics of the PET resin are not impaired.
【0015】このような共重合可能な成分としてはナフ
タレンジカルボン酸などの芳香族ジカルボン酸、アジピ
ン酸、セバシン酸などの脂肪族ジカルボン酸、ジエチレ
ングリコール、1,4−ブタンジオール、ネオペンチル
グリコール、1,4−シクロヘキサンジメタノールなど
のジオール、ポリエチレングリコール、ポリ(テトラメ
チレンオキサイド)グリコールなどのポリアルキレング
リコールなどが挙げられる。これらの共重合成分の配合
量は通常10モル%以下、好ましくは5モル%以下であ
る。Examples of such copolymerizable components include aromatic dicarboxylic acids such as naphthalenedicarboxylic acid, aliphatic dicarboxylic acids such as adipic acid and sebacic acid, diethylene glycol, 1,4-butanediol, neopentyl glycol, 1, Examples thereof include diol such as 4-cyclohexanedimethanol, polyethylene glycol, polyalkylene glycol such as poly (tetramethylene oxide) glycol, and the like. The blending amount of these copolymerization components is usually 10 mol% or less, preferably 5 mol% or less.
【0016】本発明に用いられるPET樹脂の極限粘度
は0.6〜1.0dl/g、好ましくは0.7〜0.9dl
/gである。極限粘度が0.6dl/gより低い場合は得
られるシートの機械物性が著しく低下し、耐衝撃性の十
分な向上が見られない。極限粘度が1.0dl/gより高
い場合は、樹脂流動性が悪くなりシート製膜が困難とな
る。The PET resin used in the present invention has an intrinsic viscosity of 0.6 to 1.0 dl / g, preferably 0.7 to 0.9 dl.
/ G. When the intrinsic viscosity is lower than 0.6 dl / g, the mechanical properties of the obtained sheet are remarkably deteriorated and the impact resistance is not sufficiently improved. When the intrinsic viscosity is higher than 1.0 dl / g, the resin fluidity becomes poor and it becomes difficult to form a sheet.
【0017】本発明の多層構造ポリエステルシートとは
前記のPET樹脂およびポリプロピレン樹脂組成物を通
常の製膜手段によって得た実質的に未延伸状態のシート
である。かかる未延伸状態の多層構造シートは、本発明
の組成物を押出機により溶融混合せしめた後、一般の多
層押出し用ダイから吐出せしめ冷却ドラムにより急冷す
ることにより得られる。The multilayer polyester sheet of the present invention is a substantially unstretched sheet obtained by the conventional film forming means of the PET resin and polypropylene resin composition. Such an unstretched multilayer structure sheet is obtained by melt-mixing the composition of the present invention with an extruder and then discharging it from a general multilayer extrusion die and quenching it with a cooling drum.
【0018】本発明の多層構造シートの構成は、ポリプ
ロピレン樹脂組成物からなる主構成層の両側にPET樹
脂からなる補助層がある三層シートである。そして、主
構成層と補助層の重量比率は90:10〜40:60で
あり、好ましくは80:20〜70:30である。主構
成層の重量比率が40重量%より小さい場合は、耐衝撃
性の十分な向上が見られず、又90重量%より大きい場
合は、シートの剛性が低下し、熱成形時のドローダウン
が大きくなる欠点がある。The multilayer structure sheet of the present invention is a three-layer sheet having a main constituent layer made of a polypropylene resin composition and auxiliary layers made of PET resin on both sides. The weight ratio of the main constituent layer to the auxiliary layer is 90:10 to 40:60, preferably 80:20 to 70:30. When the weight ratio of the main constituent layer is less than 40% by weight, the impact resistance is not sufficiently improved, and when it is more than 90% by weight, the rigidity of the sheet decreases and the drawdown during thermoforming is reduced. It has the drawback of becoming larger.
【0019】本発明の多層構造シートは前述の通り、ポ
リプロピレン樹脂組成物からなる主構成層の両側にPE
T樹脂からなる補助層がある三層シートであるが、両側
の補助層の割合が極端に相違すると製膜時にシート表面
の凹凸が著しくなるため好ましくなく、両側の補助層の
重量比率は40:60〜60:40の範囲とすることが
好ましい。As described above, the multilayer structure sheet of the present invention has PE on both sides of the main constituent layer made of the polypropylene resin composition.
Although it is a three-layer sheet having an auxiliary layer made of T resin, if the ratio of the auxiliary layers on both sides is extremely different, the unevenness of the sheet surface becomes remarkable during film formation, which is not preferable, and the weight ratio of the auxiliary layers on both sides is 40: The range of 60 to 60:40 is preferable.
【0020】本発明の包装容器は、本発明の多層構造シ
ートを熱成形して得られる。熱成形は、シートを加熱軟
化せしめて所望の型に押し当て型と材料の隙間にある空
気を除去し大気圧により型に密着せしめて成形する真空
成形、あるいは大気圧以上の圧縮空気によりシートを型
に密着せしめる圧空成形、および真空、圧空を併用する
成形などが適用できる。The packaging container of the present invention can be obtained by thermoforming the multilayer structure sheet of the present invention. Thermoforming is carried out by heating and softening the sheet, pressing it against the desired mold, removing the air in the gap between the mold and the material, and adhering it to the mold at atmospheric pressure, or forming the sheet by compressed air above atmospheric pressure. It is possible to apply pressure molding such that it is brought into close contact with the mold, or molding that uses vacuum and pressure together.
【0021】[0021]
【発明の効果】本発明の多層構造シートおよびそれから
なる包装容器は、優れた透明性を有し、熱成形性、二次
加工性に優れ、高温多湿度下でも耐衝撃性の経時的低下
が少なく、各種包装容器として広く使用できる。EFFECT OF THE INVENTION The multi-layered sheet of the present invention and the packaging container comprising the same have excellent transparency, excellent thermoformability and secondary processability, and their impact resistance decreases with time even under high temperature and high humidity. It is few and can be widely used as various packaging containers.
【0022】[0022]
【実施例】以下実施例により本発明を更に詳細に説明す
る。尚、実施例における主な物性値は以下に示す方法に
より測定した。 (1)極限粘度(IV) フェノール60重量%、1,1,2,2−テトラクロロ
エタン40重量%の混合溶液50mlに試料0.5gを溶
かし、20℃にて測定した。 (2)メルトフローレイト(MFR) メルトインデクサー(東洋精機製作所製)を使用し、樹
脂溶融温度230℃にてJIS−K7210に準じて測
定した。 (3)透明性(ヘーズ) 厚み300μmのシートを、JIS−K7105に従っ
て測定した。 (4)耐衝撃性 厚み300μmのシートをJIS2号形試験片に打抜
き、JIS−K7113に従って測定して得られる破断
時の伸び率(%)によって評価した。 (5)剛性(弾性率) 厚み300μmのシートをJIS2号形試験片に打抜
き、JIS−K7113に従って測定した。The present invention will be described in more detail with reference to the following examples. The main physical property values in the examples were measured by the methods described below. (1) Intrinsic viscosity (IV) 0.5 g of a sample was dissolved in 50 ml of a mixed solution of 60% by weight of phenol and 40% by weight of 1,1,2,2-tetrachloroethane, and measured at 20 ° C. (2) Melt flow rate (MFR) A melt indexer (manufactured by Toyo Seiki Seisaku-sho, Ltd.) was used and measured at a resin melting temperature of 230 ° C. according to JIS-K7210. (3) Transparency (Haze) A 300 μm thick sheet was measured according to JIS-K7105. (4) Impact resistance A sheet having a thickness of 300 µm was punched into a JIS No. 2 type test piece, and the elongation at break (%) obtained by measurement according to JIS-K7113 was evaluated. (5) Rigidity (Elastic Modulus) A sheet having a thickness of 300 μm was punched into a JIS No. 2 type test piece and measured according to JIS-K7113.
【0023】実施例1〜5、比較例1〜4 MFR値4.9g/10min のシンジオタクチックポリ
プロピレン80重量%MFR値4.0g/10min のア
イソタクチックポリプロピレン20重量%とをスクリュ
ー径30mmの二軸混練機を用いて溶融ブレンドし、MF
R値6.1g/10min のペレット状の樹脂組成物を得
た。Examples 1 to 5 and Comparative Examples 1 to 4 80% by weight of syndiotactic polypropylene having an MFR value of 4.9 g / 10 min and 20% by weight of isotactic polypropylene having an MFR value of 4.0 g / 10 min and a screw diameter of 30 mm. Melt blended using a twin-screw kneader, and MF
A pelletized resin composition having an R value of 6.1 g / 10 min was obtained.
【0024】3つの1軸押出し機を備えた幅80cmのT
ダイを有する多層シート押出し機を用い、原料として上
記の樹脂組成物を主構成層に、エチレングリコールとテ
レフタル酸からなる極限粘度が0.58dl/g、0.8
5dl/g、1.02dl/gの3種PET樹脂を補助層に
表1に示した割合で使用して厚み0.3mmの三層シート
を押出した。主構成層押出し機のシリンダー温度は23
0℃、補助層押出し機のシリンダー温度は280℃、T
ダイの温度は270℃、冷却ローラーの温度は30℃で
行った。シートの透明性(ヘーズ)、剛性(弾性率)を
測定した。80 cm wide T equipped with three single screw extruders
Using a multilayer sheet extruder having a die, the above resin composition as a raw material is used as a main constituent layer, and the intrinsic viscosity of ethylene glycol and terephthalic acid is 0.58 dl / g, 0.8
A three-layer sheet having a thickness of 0.3 mm was extruded using 3 kinds of PET resin of 5 dl / g and 1.02 dl / g as the auxiliary layer in the ratio shown in Table 1. Cylinder temperature of the main constituent layer extruder is 23
0 ℃, auxiliary layer extruder cylinder temperature 280 ℃, T
The die temperature was 270 ° C., and the cooling roller temperature was 30 ° C. The transparency (haze) and rigidity (elastic modulus) of the sheet were measured.
【0025】得られたシートを、常温放置3ヶ月に相当
する測定条件(40℃、60%RH雰囲気中に7日間)
に放置し、耐衝撃性(引張伸度)の変化を測定した。The obtained sheet was left at room temperature for 3 months under the measurement conditions (40 ° C., 60% RH atmosphere for 7 days).
Then, the change in impact resistance (tensile elongation) was measured.
【0026】このシートを単発真空熱成形機を用いて、
予熱温度300℃で内径10cm、深さ55mmの円柱状の
容器を成形し、賦形性良好な成形品を得るのに要したシ
ートの予熱時間幅で成形性を評価した。評価基準は、予
熱時間幅が10秒以上のものを(○)、10秒以下のも
のを(×)とした。Using a single-shot vacuum thermoforming machine, this sheet was
A cylindrical container having an inner diameter of 10 cm and a depth of 55 mm was formed at a preheating temperature of 300 ° C., and the formability was evaluated by the preheating time width of the sheet required to obtain a molded product having good shapeability. As the evaluation criteria, the one having a preheating time width of 10 seconds or more was (◯) and the one having a preheating time width of 10 seconds or less was (x).
【0027】得られた成形品を40℃、60%RH雰囲
気中に7日間放置した後、水を充填し、所定の高さから
底部を下にして落下させ、成形品の割れを測定した。評
価基準は、5個の成形品のうち1つも割れなかった場合
(○)、1つでも割れた場合(×)とした。以上の評
価、測定結果をまとめて表1に示す。The molded product thus obtained was allowed to stand in an atmosphere of 40 ° C. and 60% RH for 7 days, then filled with water and dropped from a predetermined height with the bottom portion down, and cracking of the molded product was measured. The evaluation standard was that no one of the five molded products cracked (◯) and one cracked (x). The above evaluation and measurement results are summarized in Table 1.
【0028】[0028]
【表1】 [Table 1]
【0029】実施例1〜3では成形品の経日、落下衝撃
テストに於ける70cm評価で各々1個の割れがあった
が、50cm以下の評価では全く割れの発生が無く、従前
のPET樹脂単独の成形品に較べ大幅な性能改善が認め
られた。実施例4、実施例5で得られたシート、及び成
形品は全ての評価、測定項目で満足すべき結果を得た。
これに対し、主構成層の重量比率が小さい比較例1では
耐衝撃性(引張伸度)の改善が無く、経日的な物性の低
下が起こった。逆に、主構成層の重量比率の大きい比較
例2ではシートの剛性(弾性率)が低く、熱成形が出来
ず、後評価に値する成形品を得ることは出来なかった。
又、比較例3のように補助層のPET樹脂の粘度が低す
ぎると、耐衝撃性(引張伸度)の改善が無く、経日的な
物性の低下が起こった。比較例4のように補助層のPE
T樹脂として、範囲外に粘度の高いものを選定するとシ
ート製膜が出来ず、後の試験に繋がらなかった。In Examples 1 to 3, there was one crack each in the 70 cm evaluation of the molded product over time and in the drop impact test, but in the evaluation of 50 cm or less, no cracking occurred at all, and the conventional PET resin was used. A significant performance improvement was observed compared to a single molded product. The sheets and molded articles obtained in Examples 4 and 5 gave satisfactory results in all evaluation and measurement items.
On the other hand, in Comparative Example 1 in which the weight ratio of the main constituent layers was small, the impact resistance (tensile elongation) was not improved and the physical properties were deteriorated over time. On the contrary, in Comparative Example 2 in which the weight ratio of the main constituent layers was large, the rigidity (elastic modulus) of the sheet was low, thermoforming could not be performed, and a molded product worthy of the later evaluation could not be obtained.
Further, when the viscosity of the PET resin of the auxiliary layer was too low as in Comparative Example 3, the impact resistance (tensile elongation) was not improved and the physical properties were deteriorated over time. PE as an auxiliary layer as in Comparative Example 4
If a resin having a high viscosity out of the range was selected as the T resin, a film could not be formed into a sheet, which did not lead to the subsequent tests.
Claims (2)
ロピレンを含有するプロピレン樹脂組成物からなる主構
成層の両側に極限粘度が0.6〜1.0dl/gのポリエ
チレンテレフタレート樹脂からなる補助層を有する多層
構造シートであって、主構成層と補助層の重量比率が9
0:10〜40:60の範囲にあることを特徴とする多
層シート及びそれからなる包装容器。1. A multilayer having a main constituent layer made of a propylene resin composition containing polypropylene having a syndiotactic structure and an auxiliary layer made of a polyethylene terephthalate resin having an intrinsic viscosity of 0.6 to 1.0 dl / g on both sides. A structural sheet in which the weight ratio of the main constituent layer and the auxiliary layer is 9
A multilayer sheet and a packaging container comprising the same, which are in the range of 0:10 to 40:60.
ロピレンを含有するプロピレン樹脂組成物がシンジオタ
クチックポリプロピレン5〜95重量部、およびアイソ
タクチックポリプロピレン95〜5重量部からなるポリ
プロピレン樹脂組成物であることを特徴とする請求項1
記載の多層構造シート及びそれからなる包装容器。2. A polypropylene resin composition containing polypropylene having a syndiotactic structure is a polypropylene resin composition comprising 5 to 95 parts by weight of syndiotactic polypropylene and 95 to 5 parts by weight of isotactic polypropylene. Claim 1 characterized by
The multilayer structure sheet described above and a packaging container made of the same.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7227457A JPH0952327A (en) | 1995-08-10 | 1995-08-10 | Multilayer sheet and packaging container made of the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7227457A JPH0952327A (en) | 1995-08-10 | 1995-08-10 | Multilayer sheet and packaging container made of the same |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0952327A true JPH0952327A (en) | 1997-02-25 |
Family
ID=16861177
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7227457A Pending JPH0952327A (en) | 1995-08-10 | 1995-08-10 | Multilayer sheet and packaging container made of the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0952327A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018043155A1 (en) * | 2016-08-30 | 2018-03-08 | 東レフィルム加工株式会社 | Protective film and laminated film |
-
1995
- 1995-08-10 JP JP7227457A patent/JPH0952327A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018043155A1 (en) * | 2016-08-30 | 2018-03-08 | 東レフィルム加工株式会社 | Protective film and laminated film |
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