JPH02215529A - Multi-layer plastic vessel superior in surface gloss property - Google Patents
Multi-layer plastic vessel superior in surface gloss propertyInfo
- Publication number
- JPH02215529A JPH02215529A JP1036057A JP3605789A JPH02215529A JP H02215529 A JPH02215529 A JP H02215529A JP 1036057 A JP1036057 A JP 1036057A JP 3605789 A JP3605789 A JP 3605789A JP H02215529 A JPH02215529 A JP H02215529A
- Authority
- JP
- Japan
- Prior art keywords
- ethylene
- resin
- layer
- random copolymer
- adhesive
- 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
Links
- 229920003023 plastic Polymers 0.000 title claims abstract description 27
- 239000004033 plastic Substances 0.000 title claims abstract description 27
- 239000010410 layer Substances 0.000 claims abstract description 73
- 229920005989 resin Polymers 0.000 claims abstract description 69
- 239000011347 resin Substances 0.000 claims abstract description 69
- 239000002344 surface layer Substances 0.000 claims abstract description 23
- 230000004888 barrier function Effects 0.000 claims abstract description 20
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000005977 Ethylene Substances 0.000 claims abstract description 18
- 239000000853 adhesive Substances 0.000 claims abstract description 17
- 229920005604 random copolymer Polymers 0.000 claims abstract description 6
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 claims abstract 4
- 229920005674 ethylene-propylene random copolymer Polymers 0.000 claims description 31
- 230000001070 adhesive effect Effects 0.000 claims description 16
- -1 polypropylene Polymers 0.000 claims description 13
- 239000004743 Polypropylene Substances 0.000 claims description 11
- 229920001155 polypropylene Polymers 0.000 claims description 11
- 239000000155 melt Substances 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 7
- 239000003208 petroleum Substances 0.000 claims description 7
- 229920005672 polyolefin resin Polymers 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 15
- 238000000071 blow moulding Methods 0.000 description 7
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 5
- 229920000219 Ethylene vinyl alcohol Polymers 0.000 description 4
- 239000012790 adhesive layer Substances 0.000 description 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 4
- 239000004840 adhesive resin Substances 0.000 description 3
- 229920006223 adhesive resin Polymers 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 229920001903 high density polyethylene Polymers 0.000 description 3
- 239000004700 high-density polyethylene Substances 0.000 description 3
- 229920001519 homopolymer Polymers 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 229920000098 polyolefin Polymers 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920005676 ethylene-propylene block copolymer Polymers 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- OFNISBHGPNMTMS-UHFFFAOYSA-N 3-methylideneoxolane-2,5-dione Chemical compound C=C1CC(=O)OC1=O OFNISBHGPNMTMS-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000251730 Chondrichthyes Species 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 125000003368 amide group Chemical group 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 150000002148 esters Chemical group 0.000 description 1
- 229920006228 ethylene acrylate copolymer Polymers 0.000 description 1
- 239000004715 ethylene vinyl alcohol Substances 0.000 description 1
- 238000005227 gel permeation chromatography Methods 0.000 description 1
- RZXDTJIXPSCHCI-UHFFFAOYSA-N hexa-1,5-diene-2,5-diol Chemical compound OC(=C)CCC(O)=C RZXDTJIXPSCHCI-UHFFFAOYSA-N 0.000 description 1
- 229920006017 homo-polyamide Polymers 0.000 description 1
- 210000000936 intestine Anatomy 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D1/00—Containers having bodies formed in one piece, e.g. by casting metallic material, by moulding plastics, by blowing vitreous material, by throwing ceramic material, by moulding pulped fibrous material, by deep-drawing operations performed on sheet material
- B65D1/02—Bottles or similar containers with necks or like restricted apertures, designed for pouring contents
- B65D1/0207—Bottles or similar containers with necks or like restricted apertures, designed for pouring contents characterised by material, e.g. composition, physical features
- B65D1/0215—Bottles or similar containers with necks or like restricted apertures, designed for pouring contents characterised by material, e.g. composition, physical features multilayered
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、多層プラスチック容器に関し、より詳細には
、優れた表面光沢を有する多層プラスチック容器に関す
る。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to multilayer plastic containers, and more particularly to multilayer plastic containers with excellent surface gloss.
(従来の技術)
プラスチック中空成形容器を、多層の積層構成とするこ
とは周知であり、この場合、容器の内外表面層としては
、衛生的特性、耐湿性等の見地からポリエチレン、ポリ
プロピレン等のポリオレフィン樹脂が使用され、また、
容器のガスバリヤ−の見地から、これら両表面層でエチ
レン−ビニルアルコール共重合体のごときガスバリヤ−
性樹脂をサンドイッチさせる積層構成が採用されている
。(Prior Art) It is well known that plastic blow-molded containers have a multi-layered laminated structure. In this case, the inner and outer surface layers of the container are made of polyolefin such as polyethylene or polypropylene from the viewpoint of hygienic properties and moisture resistance. resin is used, and
From the viewpoint of the gas barrier of the container, both surface layers are made of a gas barrier such as ethylene-vinyl alcohol copolymer.
A laminated structure is used in which the resin is sandwiched.
中空成形用のポリオレフィン樹脂には、通常の成形とは
異なったグレードのものが一般に使用されている。即ち
、中空成形に際しては、溶融パリソンが自重により垂れ
下がる現象(ドローダウンと呼ばれる)や溶融パリソン
自体に波立ちを生じたり或いはサメ肌を生じる現象(メ
ルトフラクチュア)を生じやすく、これを防止するため
に、メルトフローレート(MFR)が2.0g710分
以下でMwZMnで定義される分子量分布が広い範囲、
即ち3.5〜7の範囲にある樹脂が使用されている。こ
の樹脂は、上記ドローダウンやメルトフラクチュアの防
止には有効であるとしても、形成される器壁は表面光沢
が乏しく、また透明性に欠けており、更にビン詰製品と
した場合、ビンを通しての内容物の外観が実物よりも劣
ったものとなり、商品価値に乏しいものとなるという欠
点があり、その光沢度は高々60%程度であった。Polyolefin resins for blow molding are generally of a different grade from those used for normal molding. That is, during blow molding, a phenomenon in which the molten parison sags due to its own weight (called drawdown) or a phenomenon in which the molten parison itself becomes rippled or has a shark's skin (melt fracture) tends to occur, and in order to prevent this, , a melt flow rate (MFR) of 2.0 g 710 minutes or less and a wide range of molecular weight distribution defined by MwZMn,
That is, resins in the range of 3.5 to 7 are used. Although this resin is effective in preventing the above-mentioned drawdown and melt fracture, the formed container wall has poor surface gloss and lacks transparency. The problem was that the appearance of the contents was inferior to the actual product, and the product value was poor, and the gloss level was about 60% at most.
従って1本発明の目的は、優れた表面光沢、衛生的特性
等を有する多層プラスチック容器を提供するにある。Accordingly, one object of the present invention is to provide a multilayer plastic container having excellent surface gloss, hygienic properties, etc.
(問題点を解決するための手段)
本発明によれば、2種以上の樹脂層が積層された構造の
多層プラスチック容器において、最外表面層が、エチレ
ン含有量が2乃至8重量%で、メルトフローレートが2
.5g/10分以上で且つM w / M nの比が3
乃至5のエチレン−プロピレン・ランダム共重合体から
成ることを特徴とする表面光沢性に優れた多層プラスチ
ック容器が提供される。(Means for Solving the Problems) According to the present invention, in a multilayer plastic container having a structure in which two or more types of resin layers are laminated, the outermost surface layer has an ethylene content of 2 to 8% by weight, Melt flow rate is 2
.. 5g/10 minutes or more and the ratio of M w / M n is 3
A multilayer plastic container with excellent surface gloss is provided, which is characterized by being made of the ethylene-propylene random copolymer of 5 to 5.
(作 用)
本発明の多層プラスチック容器の一例を示す第1図にお
いて、この容器lは、胴部2、胴部2の下端に連なり、
しかもパリソンのピンチオフにより、形成された底部3
、胴部2の上端に肩部4を介して連なる口頚部5から成
ってあり、この口頭部5には蓋体(図示せず)と密封係
合される口部6及び口部6の下方のネジ、ビード、フラ
ンジ或いは段層等から成る蓋取付部7が設けられている
。(Function) In FIG. 1 showing an example of the multilayer plastic container of the present invention, the container 1 is connected to a body 2, a lower end of the body 2,
Moreover, the bottom 3 formed by pinching off the parison
, consists of a mouth and neck part 5 that is connected to the upper end of the body part 2 via a shoulder part 4, and this mouth part 5 includes a mouth part 6 that is sealingly engaged with a lid (not shown) and a lower part of the mouth part 6. A lid attachment part 7 is provided which is made of a screw, a bead, a flange, a step layer, or the like.
この多層プラスチック容器の器壁断面を拡大して示す第
2図において、この器壁は本発明のエチレン−プロピレ
ン・ランダム共重合体から成る外表面層lO及び外表面
層11及びガスバリヤ−性樹脂から成る中間層12.ポ
リオレフィン樹脂から成る基材樹脂層13から構成され
ており、これらの樹脂層が互いに接着性に乏しい場合に
は、各層間に接着剤樹脂14a、14bを介在させるこ
とができる。In FIG. 2, which shows an enlarged cross-section of the wall of this multilayer plastic container, the wall is made of an outer surface layer 10 and an outer surface layer 11 made of the ethylene-propylene random copolymer of the present invention, and a gas barrier resin. The middle layer consisting of 12. It is composed of a base resin layer 13 made of polyolefin resin, and if these resin layers have poor adhesiveness to each other, adhesive resins 14a and 14b can be interposed between each layer.
本発明の多層プラスチック容器における重要な特徴の一
つは、最外表面層にエチレン含有量が2乃至8重量%で
、メルトフローレートが2.5 g/10分以上で且つ
M w / M nの比が3乃至5のエチレン−プロピ
レン・ランダム共重合体を使用する点にある。One of the important features of the multilayer plastic container of the present invention is that the outermost surface layer has an ethylene content of 2 to 8% by weight, a melt flow rate of 2.5 g/10 minutes or more, and M w / M n The point is that an ethylene-propylene random copolymer having a ratio of 3 to 5 is used.
従来、ポリプロピレン等のポリオレフィン樹脂をこの種
の容器に用いる場合は、メルトフローレート(MFR)
が1−5g/10分以下であることが、ドローダウン防
止のために必要であった。しかし1.5g/IQ分以下
のMFRでは満足する表面光沢を得ることができなかっ
た。また、ポリブロビレンは、結晶化により透明性が悪
くなる傾向があった。Conventionally, when polyolefin resin such as polypropylene is used for this type of container, the melt flow rate (MFR)
In order to prevent drawdown, it was necessary that the amount was 1-5 g/10 minutes or less. However, with an MFR of 1.5 g/IQ min or less, a satisfactory surface gloss could not be obtained. Furthermore, polybropylene tends to have poor transparency due to crystallization.
本発明はM w / M nの比が3乃至5.特に3.
5乃至4.5の分子量分布を有すると共に、エチレン含
有量が2乃至8重量%、特に3乃至5重量%の条件を満
足するエチレン−プロピレン・ランダム共重合体とする
ことにより、このレジンを多層ボトルの外層とすること
でメルトフローレートが2.5g/10分以上、特に3
乃至5g/10分という大きい値でもドローダウンを防
止し、多層プラスチック容器の表面光沢、耐汚染性、透
明性等を顕著に改善し得るという、多層ボトルに関する
新規知見に基づくものである。In the present invention, the ratio of M w /M n is 3 to 5. Especially 3.
By using an ethylene-propylene random copolymer that has a molecular weight distribution of 5 to 4.5 and an ethylene content of 2 to 8% by weight, particularly 3 to 5% by weight, this resin can be made into a multi-layered copolymer. By making it the outer layer of the bottle, the melt flow rate is 2.5g/10 minutes or more, especially 3.
This is based on new knowledge regarding multilayer bottles that drawdown can be prevented even at large values of 5 to 5 g/10 minutes, and the surface gloss, stain resistance, transparency, etc. of multilayer plastic containers can be significantly improved.
即ち、本発明においては、 M w /M nの比(分
子量分布)が3乃至5、特に3.5乃至4.5であるこ
とが重要であり、M w / M nの比が上記範囲よ
りも大きいと゛容器表面の光沢が失われ、また上記範囲
よりも小さいと成形容器の器壁がシャークスキンとなっ
てしまうのである。この分子量分布は、ゲルパーミュエ
ーションクロマトグラフ法を用いて分子量分布曲線を求
めポリスチレンをスタンダードとしてユニバーサルキャ
リブレーション法により重量平均分子量と数平均分子量
とを算出することにより求め得る。That is, in the present invention, it is important that the ratio of M w /M n (molecular weight distribution) is 3 to 5, particularly 3.5 to 4.5, and that the ratio of M w / M n is less than the above range. If it is too large, the surface of the container will lose its luster, and if it is smaller than the above range, the wall of the molded container will become sharkskin. This molecular weight distribution can be determined by obtaining a molecular weight distribution curve using gel permeation chromatography and calculating the weight average molecular weight and number average molecular weight using a universal calibration method using polystyrene as a standard.
更に、このエチレン−プロピレン・ランダム共重合体の
エチレン含有量が2乃至8重量%、特に3乃至5重量%
であることも重要である。上記範囲よりもエチレン含有
量が少ないと、容器表面の光沢が低下し、また上記範囲
よりも多いと器壁が柔らかすぎて傷が付きやすく、且つ
剛性にも劣るようになる。Furthermore, the ethylene content of this ethylene-propylene random copolymer is 2 to 8% by weight, particularly 3 to 5% by weight.
It is also important that If the ethylene content is less than the above range, the gloss of the container surface will decrease, and if it is more than the above range, the container wall will be too soft and easily scratched, and the rigidity will be poor.
また、このエチレン−プロピレン・ランダム共重合体の
メルトフローレート(MFR)が2.5g/10分以上
、特に3乃至5g/10分であることも容器の成形性の
点で重要である。即ち、メルトフローレートが上記範囲
よりも小さいと、流動性が悪く押出時の負荷が大きくな
ると、金型賦型性が悪くなると共に光沢が失われる。ま
た、上記範囲よりも大きいMFRを有するものは、多層
ポルの一部として前記範囲内で使用してもドローダウン
が大きく中空成形が一般に困難となり、また耐衝撃性に
劣るようになる。It is also important from the viewpoint of moldability of the container that the melt flow rate (MFR) of this ethylene-propylene random copolymer is 2.5 g/10 minutes or more, particularly 3 to 5 g/10 minutes. That is, if the melt flow rate is lower than the above range, the fluidity will be poor and if the load during extrusion becomes large, the moldability will deteriorate and the gloss will be lost. Furthermore, a material having an MFR larger than the above range will have large drawdown even if used as part of a multilayer polyester within the above range, making blow molding generally difficult, and will also have poor impact resistance.
本発明は、これらの条件を満足するエチレン−プロピレ
ン・ランダム共重合体を最外表面層を構成する樹脂とし
て使用することにより、得られる多層プラスチック容器
は、優れた表面光沢度を有し、光沢度(JIS K 7
105に準拠、入射角60°)が8°ぢ%と、ポリカー
ボネートやポリエステルボトルで得られる光沢度と同程
度の表面光沢を有している。In the present invention, by using an ethylene-propylene random copolymer that satisfies these conditions as a resin constituting the outermost surface layer, the resulting multilayer plastic container has excellent surface gloss and gloss. degree (JIS K 7
105, the incident angle (60°) is 8°㎢%, which is the same level of surface gloss as that obtained from polycarbonate or polyester bottles.
(発明の好適態様)
本発明においては、上記エチレン−プロピレン・ランダ
ム共重合体の代わりに、水素添加石油樹脂を5乃至25
重量%、特にlO乃至20重量%含有するエチレン−プ
ロピレン・ランダム共重合体を用いることも可能である
。この水素添加石油樹脂は、無色透明、無臭であり、耐
熱性、耐候性等に優れた樹脂である。この樹脂を上記エ
チレン−プロピレン・ランダム共重合体の代わりに最外
表面層に用いると同様の効果を得ることができる。この
水素添加石油樹脂としては1例えばアルコンP−140
(荒川化学工業株式会社製)を好適に用いることができ
る。(Preferred embodiment of the invention) In the present invention, hydrogenated petroleum resin is used in place of the above ethylene-propylene random copolymer.
It is also possible to use ethylene-propylene random copolymers containing 10% by weight, in particular 10 to 20% by weight. This hydrogenated petroleum resin is colorless, transparent, odorless, and has excellent heat resistance, weather resistance, etc. Similar effects can be obtained by using this resin in the outermost surface layer instead of the ethylene-propylene random copolymer. As this hydrogenated petroleum resin, 1, for example, Alcon P-140
(manufactured by Arakawa Chemical Industry Co., Ltd.) can be suitably used.
本発明に用いるエチレン−プロピレン・ランダム共重合
体は、それ自体成形性が悪く、この樹脂と成形性に優れ
た基材樹脂とを組合せることが必要である。この基材樹
脂としては、オレフィン樹脂が好適であり、中でもポリ
プロピレンや高密度ポリエチレン等を用いることができ
る。The ethylene-propylene random copolymer used in the present invention itself has poor moldability, and it is necessary to combine this resin with a base resin having excellent moldability. As this base resin, olefin resin is suitable, and among them, polypropylene, high density polyethylene, etc. can be used.
ボリブロレピンとしては、プロピレンの単独重合体であ
ってもよく、またプロピレンとエチレン或いは他のα−
オレフィン、例えば、ブテン−1、ペンテン−1、ヘキ
セン−1等との共重合体であってもよく、更にこれらの
2種以上のブレンド物であってもよい、これらの単独重
合体或いはブレンド物は、X線回折学的にいって結晶性
であるべきであり、また重合体全体当りのプロピレン単
位の含有量は85モル%以上、特に90モル%以上、ま
たメルトフローレートがボリブロビレンの場合は2g/
10分以下であるべきである。Voribrolepin may be a homopolymer of propylene, or it may be a homopolymer of propylene and ethylene or other α-
It may be a copolymer with olefin, for example, butene-1, pentene-1, hexene-1, etc., or it may be a blend of two or more of these, or a homopolymer or blend thereof. should be crystalline in terms of X-ray diffraction, and the content of propylene units in the entire polymer should be 85 mol% or more, especially 90 mol% or more, and if the melt flow rate is polypropylene, 2g/
Should be no more than 10 minutes.
また、ポリオレフィン樹脂の他の例としては、MFRo
、5以下の高密度ポリエチレンを用いることができる。In addition, other examples of polyolefin resins include MFRo
, 5 or less can be used.
この場合接着剤が必要であり、接着剤としては、リニア
低密度ポリエチレン、エチレンアクリル酸エステルコポ
リマーが適当である。In this case, an adhesive is required, and suitable adhesives include linear low density polyethylene and ethylene acrylate copolymer.
この高密度ポリエチレンもドローダウン性防止の点で、
0.5g710分以下のメルトフローレートを有するべ
きである。This high-density polyethylene also has the advantage of preventing drawdown.
It should have a melt flow rate of less than 0.5g710min.
本発明に用いるポリオレフィン樹脂は、その主体となる
樹脂が前述したポリプロピレン及び/または高密度ポリ
エチレンである範囲内で、他の樹脂例えば他のオレフィ
ン樹脂等を含有していても同等差支えない、また、スク
ラップ樹脂等をポリオレフィン樹脂に配合することもで
き、スクラップ樹脂を単独の層として設けることもでき
る。The polyolefin resin used in the present invention may contain other resins, such as other olefin resins, as long as the main resin is the above-mentioned polypropylene and/or high-density polyethylene. A scrap resin or the like may be blended with the polyolefin resin, or the scrap resin may be provided as a single layer.
本発明において、ガスバリヤ−性樹脂としては、一般に
酸素透過係数(Pot)が5.5 Xl0−” cc−
Cs7cm”sec−cmHg以下、特に4.5 xt
o−” cc−c+++/Cm!・5ec−c+mHg
以下で、しかも上述した透明性な有するものが好適に使
用され、特にエチレン含有量が20乃至50モル%で且
つ未ケン化ビニルエステル残基の含有量が5モル%以下
のエチレン−ビニルアルコール共重合体や、炭素数10
0個当りのアミド基の数が3乃至30個、特に4乃至2
5個の範囲で含有されるホモポリアミド、コポリアミド
またはそのブレンド物が好適に使用される。In the present invention, the gas barrier resin generally has an oxygen permeability coefficient (Pot) of 5.5 Xl0-" cc-
Cs7cm”sec-cmHg or less, especially 4.5 xt
o-" cc-c+++/Cm!・5ec-c+mHg
In the following, those having the above-mentioned transparency are preferably used, especially ethylene-vinyl alcohol having an ethylene content of 20 to 50 mol% and a content of unsaponified vinyl ester residues of 5 mol% or less. Polymer or carbon number 10
The number of amide groups per 0 is 3 to 30, especially 4 to 2
Homopolyamides, copolyamides or blends thereof containing in the range of 5 are preferably used.
勿論、上述したエチレン−ビニルアルコール共重合体と
ポリアミドとはブレンド物の形で使用することもできる
し、このものの本質を損なわない範囲内、例えば20重
量%以下の範囲内で、他の熱可塑性樹脂、例えばポリオ
レフィンやポリオレフィンとの間の接着性を付与する樹
脂等をブレンドとして用いることもできる。Of course, the above-mentioned ethylene-vinyl alcohol copolymer and polyamide can be used in the form of a blend, and other thermoplastics can be used within a range that does not impair the essence of the product, for example, within a range of 20% by weight or less. Blends of resins, such as polyolefins and resins that provide adhesion to polyolefins, can also be used.
なお、ガスバリヤ−性樹脂としては、用いる内外表面層
との屈折率の差の絶対値が0.1以下であることが好ま
しく、最も好適には内外表面層の屈折率と同等の屈折率
を有するガスバリヤ−性樹脂の使用が好ましい。The gas barrier resin preferably has an absolute value of the difference in refractive index between the inner and outer surface layers of 0.1 or less, and most preferably has a refractive index equivalent to that of the inner and outer surface layers. Preferably, a gas barrier resin is used.
ガスバリヤ−性樹脂と、内外表面層との間に接着性がな
い場合には、両横脂層の間に、酸変性オレフィン樹脂1
例えば無水マレイン酸、アクリル酸、メタクリル酸、無
水イタコン酸等のエチレン系不飽和カルボン酸乃至はそ
の無水物でグラフト変性されたポリエチレン、ポリプロ
ピレン等の接着剤層を介在させることが好ましい、この
接着剤層を介在させる代わりに、上述した樹脂をガスバ
リヤ−層や内外表面層の少なくとも一方に含有させるこ
とができる。If there is no adhesion between the gas barrier resin and the inner and outer surface layers, add 1 acid-modified olefin resin between both side resin layers.
For example, it is preferable to interpose an adhesive layer of polyethylene, polypropylene, or the like graft-modified with an ethylenically unsaturated carboxylic acid such as maleic anhydride, acrylic acid, methacrylic acid, or itaconic anhydride or its anhydride. Instead of interposing a layer, the above-mentioned resin can be contained in at least one of the gas barrier layer and the inner and outer surface layers.
本発明の多層プラスチック容器器壁の層構成は、外層か
ら前記エチレン−プロピレンランダム共重合体/基材樹
脂、またガスバリヤ−性を向上させる場合には、透明な
ボトルを得ようとする場合は、外層から内層に向かって
順に前記エチレン−プロピレン・ランダム共重合体/接
着剤/ガスバリヤ−性樹脂/接着剤/基材樹脂、スクラ
ップ樹脂を利用する場合は、外層から内層に向かって順
に前記エチレン−プロピレン・ランダム共重合体/スク
ラップ樹脂/接着剤/ガスバリヤ−性樹脂/接着剤/基
材樹脂の層構成とすることにより、それぞれ表面光沢に
優れた多層プラスチック容器を得ることが可能となる。The layer structure of the multilayer plastic container wall of the present invention includes the above-mentioned ethylene-propylene random copolymer/base resin from the outer layer, and in the case of improving gas barrier properties, and in the case of obtaining a transparent bottle, When using the ethylene-propylene random copolymer/adhesive/gas barrier resin/adhesive/base resin and scrap resin in order from the outer layer to the inner layer, the ethylene-propylene random copolymer/adhesive/gas barrier resin/adhesive/base resin and scrap resin are used in order from the outer layer to the inner layer. The layered structure of propylene random copolymer/scrap resin/adhesive/gas barrier resin/adhesive/base resin makes it possible to obtain a multilayer plastic container each having excellent surface gloss.
これらの樹脂の積層構成は、前述の層構成のものに限定
されず、種々の変更が可能であることは勿論である。It goes without saying that the laminated structure of these resins is not limited to the layered structure described above, and various changes can be made.
この最外表面層は全体の厚みの3乃至40%、特に5乃
至30%の厚み比であることも重要である。即ち、上記
範囲よりも厚み比が大きいと成形性が悪くなり、また、
上記範囲よりも厚み比が小さいと十分な表面光沢が期待
できない。It is also important that this outermost surface layer has a thickness ratio of 3 to 40%, especially 5 to 30%, of the total thickness. That is, if the thickness ratio is larger than the above range, the moldability will deteriorate, and
If the thickness ratio is smaller than the above range, sufficient surface gloss cannot be expected.
また、基材樹脂は全体の厚みの50乃至90%、特に6
0乃至70%、ガスバリヤ−性樹脂は2乃至15%、特
に3乃至10%の厚み比であることが好ましい、また、
最終容器として、器壁の厚みが0.3乃至1.5 ar
m、特に0.5乃至1.2 m腸の範囲となるように定
めるのがよい。In addition, the base resin accounts for 50 to 90% of the total thickness, especially 6
The thickness ratio is preferably 0 to 70%, and the gas barrier resin is preferably 2 to 15%, particularly 3 to 10%.
As the final container, the thickness of the vessel wall is 0.3 to 1.5 ar
m, preferably within the range of 0.5 to 1.2 m intestine.
本発明によれば1例えばエチレン−プロピレン・ランダ
ム共重合体を最外表面層、ガスバリヤ−性樹脂を中間層
、基材樹脂を内層とし、必要あれば接着性樹脂や、最内
表面層にエチレンーブロビレン・ランダム共重合体を設
けて、多重ダイを通してパリソンの形に共押出するが、
この際順守すべき制限がある。According to the present invention, 1, for example, an ethylene-propylene random copolymer is used as the outermost surface layer, a gas barrier resin is used as the intermediate layer, a base resin is used as the inner layer, and if necessary, adhesive resin or ethylene is used as the innermost surface layer. -Providing a brobylene random copolymer and coextruding it through multiple dies in the form of a parison,
There are restrictions that must be observed at this time.
先ず、このエチレン−プロピレン・ランダム共重合体か
ら、これを外表面とした中空成形用パリソンを製造する
に際して、この樹脂を混線タイプのスクリューを介して
溶融混線を行なうことが重要である。前述した分子量分
布を有するエチレン−プロピレン・ランダム共重合体で
は、パリソンの押出しが困難であり、スムーズな表面を
備えたパリソンへの押出しを可能にするためには、樹脂
中の溶融ムラを防止する必要があり、そのためには樹脂
温度を200乃至230℃の温度に均一化する必要があ
る。更に、押出機の可塑化部で生じやすい圧力変動をも
押えることも必要となり、例えば、この可塑化部での圧
力変動を、プラス・マイナス3%以下に押える必要があ
る0本発明においては、エチレン−プロピレン・ランダ
ム共重合体の溶融押出を、混線型スクリュー、例えばダ
ルメージ型スクリュー、ビン打ちスクリューを備えた押
出機を用いて行うことにより、上述した樹脂温度の均−
化及び圧力変動の防止が可能となり、表面平滑性や透明
性等に優れた中空成形容器の製造が可能となるものであ
る。混線型スクリュー以外のスクリュー、例えばメタ−
リング型スクリューを用いた場合には、本発明の中空成
形容器の製造は困難である。First, when manufacturing a parison for blow molding using this ethylene-propylene random copolymer as an outer surface, it is important to melt and cross-mix this resin through a cross-wire type screw. It is difficult to extrude parisons with the ethylene-propylene random copolymer having the above-mentioned molecular weight distribution, and in order to enable extrusion into parisons with smooth surfaces, it is necessary to prevent uneven melting in the resin. For this purpose, it is necessary to equalize the resin temperature to 200 to 230°C. Furthermore, it is also necessary to suppress pressure fluctuations that tend to occur in the plasticizing section of the extruder. For example, in the present invention, it is necessary to suppress pressure fluctuations in the plasticizing section to below +/-3%. By performing melt extrusion of the ethylene-propylene random copolymer using an extruder equipped with a mixed screw, such as a Dalmage type screw or a bottled screw, the above-mentioned uniform resin temperature can be achieved.
This makes it possible to prevent oxidation and pressure fluctuations, and to manufacture blow-molded containers with excellent surface smoothness, transparency, etc. Screws other than mixed type screws, e.g.
When a ring-type screw is used, it is difficult to manufacture the blow-molded container of the present invention.
上述した混線タイプのスクリューを用いる以外に、少な
くとも出口近傍のダイス表面の研磨もグイラインの発生
を防ぐため極めて重要となる。また金型面の研磨も重要
な要素である。In addition to using the above-mentioned cross-conductor type screw, it is also extremely important to polish the die surface at least near the exit in order to prevent the occurrence of guilines. Polishing the mold surface is also an important factor.
本発明においては、ダイスから押出されたパリソンを直
接割金型でピンチオフしてブロー成形する代わりに、押
出されたパリソンを冷風との接触や冷却金型との接触に
よって、パリソンの表面が融点よりも低いが、パリソン
の壁部中心が融点以上の温度に未だあるように冷却し、
次いでこのパリソンをブロー成形に付することも可能で
ある。In the present invention, instead of directly pinching off the parison extruded from the die with a split mold and blow molding, the extruded parison is brought into contact with cold air or with a cooling mold so that the surface of the parison rises above the melting point. Although the temperature is low, the parison is cooled so that the center of the wall is still at a temperature above the melting point.
It is also possible to then subject this parison to blow molding.
この場合には、形成されるボトル表面にはブローによる
膨張で若干の分子配向が付与されることになる。In this case, the surface of the bottle to be formed will have some molecular orientation due to the expansion caused by blowing.
(発明の効果)
本発明によれば、2種以上の樹脂層が積層された構造の
多層プラスチック容器において、最外表面層に、エチレ
ン含有量が2乃至8重量%で、メルトフローレートが2
.5g/10分以上で且つM w / M nの比が3
乃至5のエチレン−プロピレン・ランダム共重合体を用
いることにより、成形性が悪いとされていた前記樹脂を
用いた容器の成形を可能にし、且つ容器の表面光沢を光
沢度0(JIS Z 7105 入射角60°)で8
5%以上にも向上させることが可能となるのである。(Effects of the Invention) According to the present invention, in a multilayer plastic container having a structure in which two or more resin layers are laminated, the outermost surface layer has an ethylene content of 2 to 8% by weight and a melt flow rate of 2.
.. 5g/10 minutes or more and the ratio of M w / M n is 3
By using the ethylene-propylene random copolymer of 5 to 5, it is possible to mold a container using the resin, which was considered to have poor moldability, and the surface gloss of the container can be reduced to 0 (JIS Z 7105 incident light). 8 at an angle of 60°)
This makes it possible to improve it by more than 5%.
(実施例) 本発明を次の実施例で説明する。(Example) The invention is illustrated in the following examples.
実施例1
外層としてメルトフローレート(MFR)3.0g/1
0分、分子量分布(M w /M n ) 3.5 、
エチレン含有量4モル%のエチレン−プロピレンランダ
ム共重合体を外層用押出機に供給し、内層としてMFR
l、5 g/I 0分、 M w /Mn 2.0 、
エチレン含有量3.5モル%のエチレン−プロピレンブ
ロック共重合体を内層用押出機に供給して、2層溶融パ
リソンを押出し、このパリソンをブロー金型内でブロー
成形して胴部平均肉厚800μ、内容積500ccのボ
トルを得た。Example 1 Melt flow rate (MFR) 3.0g/1 as outer layer
0 minutes, molecular weight distribution (M w /M n ) 3.5,
An ethylene-propylene random copolymer with an ethylene content of 4 mol% was fed to an extruder for the outer layer, and the MFR was used as the inner layer.
l, 5 g/I 0 min, M w /Mn 2.0,
An ethylene-propylene block copolymer with an ethylene content of 3.5 mol% is supplied to an extruder for inner layer to extrude a two-layer molten parison, and this parison is blow-molded in a blow mold to obtain an average wall thickness of the body. A bottle with a diameter of 800 μm and an internal volume of 500 cc was obtained.
このボトルの各層の厚みは、外層が100u、内層が7
00μであった。The thickness of each layer of this bottle is 100U for the outer layer and 7U for the inner layer.
It was 00μ.
実施例2
実施例1の外層のエチレン−プロピレンランダム共重合
体に水素添加石油樹脂アルコンp −140(荒用化学
工業■製)を10重量%添加した以外は、実施例1と同
様にして胴部平均肉厚800u、内容積500ccのボ
トルを成形した。Example 2 A shell was made in the same manner as in Example 1, except that 10% by weight of hydrogenated petroleum resin Alcon P-140 (manufactured by Arayo Kagaku Kogyo ■) was added to the ethylene-propylene random copolymer of the outer layer of Example 1. A bottle with an average wall thickness of 800 u and an internal volume of 500 cc was molded.
このボトルの各層の厚みは、外層が40μ、内層が76
0μであった。The thickness of each layer of this bottle is 40μ for the outer layer and 76μ for the inner layer.
It was 0μ.
実施例3
実施例1の外層と内層との間にスクラップ樹脂層を形成
させた以外は実施例1と同様にして胴部平均肉厚800
μ、内容積500ccのボトルを成形した。Example 3 The average wall thickness of the body was 800 in the same manner as in Example 1 except that a scrap resin layer was formed between the outer layer and the inner layer of Example 1.
A bottle with an internal volume of 500 cc was molded.
このボトルの各層の厚みは、外層が40μ、スクラップ
層が560μ、内層が200μであった。The thickness of each layer of this bottle was 40μ for the outer layer, 560μ for the scrap layer, and 200μ for the inner layer.
実施例4
外層としてMFR3,5g/l 0分、M w / M
n4、ロ、エチレン含有量4モル%のエチレン−プロ
ピレンランダム共重合体を外層用押出機、内層としてM
FRl、9 g/l 0分、My/Mn 2.5 、
エチレン含有量3モル%のエチレン−プロピレンランダ
ム共重合体を外層用押出機、中間層としてエチレン含有
量32モル%のエチレン−ビニルアルコール共重合体か
ら成るガスバリヤ−性樹脂を中間層用押出機及び内、外
層と中間層との間に介在する接着剤層としてカルボニル
基濃度80ミリモル/10g重合体のカルボン酸変性ポ
リプロピレンを接着剤層用押出機にそれぞれ供給して溶
融パリソンを押出し、このパリソンをブロー金型内でブ
ロー成形して、胴部平均肉厚1.Otmm、内容積10
00ccのボトルを得た。Example 4 MFR3.5g/l as outer layer 0 min, Mw/M
n4, B, an ethylene-propylene random copolymer with an ethylene content of 4 mol% was used as an extruder for the outer layer, and as an inner layer M
FRl, 9 g/l 0 min, My/Mn 2.5,
An extruder for the outer layer was made of an ethylene-propylene random copolymer with an ethylene content of 3 mol%, and an extruder for the intermediate layer was used for the gas barrier resin made of an ethylene-vinyl alcohol copolymer with an ethylene content of 32 mol%. As the adhesive layer interposed between the inner and outer layers and the intermediate layer, carboxylic acid-modified polypropylene with a carbonyl group concentration of 80 mmol/10 g polymer was supplied to an extruder for the adhesive layer, and a molten parison was extruded. Blow molding is performed in a blow mold, and the average wall thickness of the body is 1. Otmm, internal volume 10
A 00cc bottle was obtained.
このボトルの各層の厚みは、外層から内層に向かって2
00μ/15μ/35μ/15μ/735μであった。The thickness of each layer of this bottle is 2 from the outer layer to the inner layer.
00μ/15μ/35μ/15μ/735μ.
実施例5
実施例3の外層のエチレン−プロピレンランダム共重合
体に前記アルコンp−140を15重量%添加し、内層
と接着剤層との間にスクラップ樹脂層を形成させた以外
は実施例3と同様にして胴部平均肉厚450μ、内容積
100ccのボトルを成形した。Example 5 Example 3 except that 15% by weight of Alcon P-140 was added to the ethylene-propylene random copolymer of the outer layer of Example 3, and a scrap resin layer was formed between the inner layer and the adhesive layer. In the same manner as above, a bottle having an average body wall thickness of 450 μm and an internal volume of 100 cc was molded.
このボトルの各層の厚みは外層から内層に向かって80
μ/10μ/20μ/10μ/230μ/100μであ
った。The thickness of each layer of this bottle is 80mm from the outer layer to the inner layer.
μ/10μ/20μ/10μ/230μ/100μ.
比較例1
MFRl、5 g/I 0分、M w /Mn 2.0
、エチレン含有量3.5モル%のエチレン−プロピレ
ンブロック共重合体を押出機に供給して溶融パリソンを
押出し、このパリソンをブロー金型内でブロー成形して
胴部平均肉厚800μ、内容積500ccのボトルを得
た。Comparative Example 1 MFRl, 5 g/I 0 min, M w /Mn 2.0
, an ethylene-propylene block copolymer with an ethylene content of 3.5 mol% is fed to an extruder to extrude a molten parison, and this parison is blow-molded in a blow mold to have a body with an average wall thickness of 800μ and an internal volume. A 500cc bottle was obtained.
比較例2
外層としてMFRl、Og/l 0分、M v / M
n6.0、エチレン含有量3.5モル%のエチレン−
プロピレンブロック共重合体を用いた以外は実施例1と
同様にしてボトルを成形した。Comparative Example 2 MFRl as outer layer, Og/l 0 min, Mv/M
n6.0, ethylene content 3.5 mol% ethylene-
A bottle was molded in the same manner as in Example 1 except that a propylene block copolymer was used.
これらの結果を表1に示す。These results are shown in Table 1.
表table
第1図は、本発明の多層ブラスチッ
例を示し、
第2図は、第1図の多層ブラスチッ
壁の拡大断面図を示す。
り容器の−
り容器の器
l・・・容器、2・・・胴部、3・・・底部、4・・・
肩部、5・・・口頚部、6・・・口部、7・・・蓋取付
部、lO・・・外表面層、11・・・内表面層、12・
・・中間層、13−・・基材樹脂層、14a、14b・
・・接着剤樹脂層。FIG. 1 shows an example of a multi-layered plastic stitch according to the invention, and FIG. 2 shows an enlarged cross-sectional view of the multi-layered plastic wall of FIG. Container container L...container, 2...body, 3...bottom, 4...
Shoulder part, 5... Mouth and neck part, 6... Mouth part, 7... Lid attachment part, lO... Outer surface layer, 11... Inner surface layer, 12.
・Intermediate layer, 13-・Base resin layer, 14a, 14b・
...Adhesive resin layer.
Claims (7)
チック容器において、最外表面層が、エチレン含有量が
2乃至8重量%で、メルトフローレートが2.5g/1
0分以上で且つ@M@w/@M@nの比が3乃至5のエ
チレン−プロピレン・ランダム共重合体から成ることを
特徴とする表面光沢性に優れた多層プラスチック容器。(1) In a multilayer plastic container having a structure in which two or more resin layers are laminated, the outermost surface layer has an ethylene content of 2 to 8% by weight and a melt flow rate of 2.5 g/1
A multilayer plastic container with excellent surface gloss, characterized in that it is made of an ethylene-propylene random copolymer that lasts for at least 0 minutes and has a @M@w/@M@n ratio of 3 to 5.
脂を含有するエチレン−プロピレン・ランダム共重合体
組成物から成る請求項1記載の多層プラスチック容器。2. The multilayer plastic container of claim 1, wherein the outermost surface layer comprises an ethylene-propylene random copolymer composition containing 5 to 25% by weight of hydrogenated petroleum resin.
で存在する請求項1記載の多層プラスチック容器。(3) The multilayer plastic container according to claim 1, wherein the outermost surface layer is present at a thickness ratio of 3 to 30% of the total thickness.
順に請求項1記載のエチレン−プロピレン・ランダム共
重合体/接着剤/ガスバリヤー性樹脂/接着剤/ポリプ
ロピレンである多層プラスチック容器。(4) A multilayer plastic container, in which the laminated structure of the container wall is, in order from the outer layer to the inner layer, the ethylene-propylene random copolymer/adhesive/gas barrier resin/adhesive/polypropylene according to claim 1.
順に請求項2記載の水素添加石油樹脂を含有するエチレ
ンプロピレン・ランダム共重合体/接着剤/ガスバリヤ
ー性樹脂/接着剤/ポリプロピレンである多層プラスチ
ック容器。(5) The laminated structure of the container wall is an ethylene propylene random copolymer containing the hydrogenated petroleum resin according to claim 2 in order from the outer layer to the inner layer/adhesive/gas barrier resin/adhesive/polypropylene. A multilayer plastic container.
に請求項1記載のエチレン−プロピレン・ランダム共重
合体/接着剤/ガスバリヤー性樹脂/接着剤/ポリプロ
ピレン+スクラップ樹脂/前記エチレン−プロピレン・
ランダム共重合体である多層プラスチック容器。(6) The laminated structure of the container wall is arranged in order from the outer layer to the inner layer: ethylene-propylene random copolymer according to claim 1 / adhesive / gas barrier resin / adhesive / polypropylene + scrap resin / Ethylene-propylene
A multilayer plastic container that is a random copolymer.
順に請求項1記載の水素添加石油樹脂を含有するエチレ
ン−プロピレン・ランダム共重合体/接着剤/ガスバリ
ヤー性樹脂/接着剤/ポリプロピレン+スクラップ樹脂
/前記エチレン−プロピレン・ランダム共重合体である
多層プラスチック容器。(7) The laminated structure of the container wall is an ethylene-propylene random copolymer containing the hydrogenated petroleum resin according to claim 1 in order from the outer layer to the inner layer/adhesive/gas barrier resin/adhesive/ A multilayer plastic container made of polypropylene + scrap resin/the ethylene-propylene random copolymer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3605789A JPH0717042B2 (en) | 1989-02-17 | 1989-02-17 | Multi-layer plastic container with excellent surface gloss |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3605789A JPH0717042B2 (en) | 1989-02-17 | 1989-02-17 | Multi-layer plastic container with excellent surface gloss |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02215529A true JPH02215529A (en) | 1990-08-28 |
JPH0717042B2 JPH0717042B2 (en) | 1995-03-01 |
Family
ID=12459090
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3605789A Expired - Fee Related JPH0717042B2 (en) | 1989-02-17 | 1989-02-17 | Multi-layer plastic container with excellent surface gloss |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0717042B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5230934A (en) * | 1991-02-27 | 1993-07-27 | Toyo Seikan Kaisha Ltd. | Frosted container |
JPH0672422A (en) * | 1992-08-21 | 1994-03-15 | Kureha Chem Ind Co Ltd | Resin bottle |
EP0604239A1 (en) * | 1992-12-25 | 1994-06-29 | Toyo Seikan Kaisha Limited | Blow-molded multi-layer containers having excellent surface luster and process for producing the same |
EP0644035A1 (en) * | 1993-09-16 | 1995-03-22 | Owens-Illinois Plastic Products Inc. | Coextruded multilayer plastic container utilizing post consumer plastic |
JPH0839743A (en) * | 1994-05-27 | 1996-02-13 | Kureha Plast Kk | Multilayer hollow plastic container |
US5888636A (en) * | 1995-01-19 | 1999-03-30 | Mitsui Chemicals, Inc. | Multi-layer blow molded article of polypropylene |
EP0904925A4 (en) * | 1996-04-18 | 2000-12-27 | Nippon Steel Chemical Co | Multi-layered blow molded body and multi-layered blow molding method |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003054591A (en) * | 2001-08-13 | 2003-02-26 | Nippon Synthetic Chem Ind Co Ltd:The | Squeezing multi-layered container |
JP2003063542A (en) * | 2001-08-23 | 2003-03-05 | Nippon Synthetic Chem Ind Co Ltd:The | Squeezing-out multi-layer container |
JP4734841B2 (en) * | 2003-11-25 | 2011-07-27 | 東洋製罐株式会社 | Multi-layer plastic container |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52114682A (en) * | 1976-03-24 | 1977-09-26 | Mitsubishi Petrochem Co Ltd | Manufacture of polypropylene laminates |
JPS5711052A (en) * | 1980-06-24 | 1982-01-20 | Kureha Chemical Ind Co Ltd | Multilayer bottle |
JPS59215864A (en) * | 1983-05-25 | 1984-12-05 | 株式会社ジェイエスピー | Manufacture of multilayer structure material |
JPS6024946A (en) * | 1983-07-21 | 1985-02-07 | 昭和電工株式会社 | Polypropylene multilayer transparent vessel |
JPS6049940A (en) * | 1983-08-31 | 1985-03-19 | 東洋製罐株式会社 | Hollow molded vessel and manufacture thereof |
JPS6049939A (en) * | 1983-08-31 | 1985-03-19 | 東洋製罐株式会社 | Transparent blow molding vessel and manufacture thereof |
JPS61202842A (en) * | 1985-03-05 | 1986-09-08 | 昭和電工株式会社 | Plastic vessel |
-
1989
- 1989-02-17 JP JP3605789A patent/JPH0717042B2/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52114682A (en) * | 1976-03-24 | 1977-09-26 | Mitsubishi Petrochem Co Ltd | Manufacture of polypropylene laminates |
JPS5711052A (en) * | 1980-06-24 | 1982-01-20 | Kureha Chemical Ind Co Ltd | Multilayer bottle |
JPS59215864A (en) * | 1983-05-25 | 1984-12-05 | 株式会社ジェイエスピー | Manufacture of multilayer structure material |
JPS6024946A (en) * | 1983-07-21 | 1985-02-07 | 昭和電工株式会社 | Polypropylene multilayer transparent vessel |
JPS6049940A (en) * | 1983-08-31 | 1985-03-19 | 東洋製罐株式会社 | Hollow molded vessel and manufacture thereof |
JPS6049939A (en) * | 1983-08-31 | 1985-03-19 | 東洋製罐株式会社 | Transparent blow molding vessel and manufacture thereof |
JPS61202842A (en) * | 1985-03-05 | 1986-09-08 | 昭和電工株式会社 | Plastic vessel |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5230934A (en) * | 1991-02-27 | 1993-07-27 | Toyo Seikan Kaisha Ltd. | Frosted container |
JPH0672422A (en) * | 1992-08-21 | 1994-03-15 | Kureha Chem Ind Co Ltd | Resin bottle |
EP0604239A1 (en) * | 1992-12-25 | 1994-06-29 | Toyo Seikan Kaisha Limited | Blow-molded multi-layer containers having excellent surface luster and process for producing the same |
US5443868A (en) * | 1992-12-25 | 1995-08-22 | Toyo Seikan Kaisha Ltd. | Blow-molded multi-layer containers having excellent surface luster and process for producing the same |
AU672057B2 (en) * | 1992-12-25 | 1996-09-19 | Toyo Seikan Kaisha Ltd. | Blow-molded multi-layer containers having excellent surface luster and process for producing the same |
EP0644035A1 (en) * | 1993-09-16 | 1995-03-22 | Owens-Illinois Plastic Products Inc. | Coextruded multilayer plastic container utilizing post consumer plastic |
JPH0839743A (en) * | 1994-05-27 | 1996-02-13 | Kureha Plast Kk | Multilayer hollow plastic container |
US5888636A (en) * | 1995-01-19 | 1999-03-30 | Mitsui Chemicals, Inc. | Multi-layer blow molded article of polypropylene |
EP0904925A4 (en) * | 1996-04-18 | 2000-12-27 | Nippon Steel Chemical Co | Multi-layered blow molded body and multi-layered blow molding method |
Also Published As
Publication number | Publication date |
---|---|
JPH0717042B2 (en) | 1995-03-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5230934A (en) | Frosted container | |
US6677013B1 (en) | Transparent multilayer polypropylene container with barrier protection | |
JPH02215529A (en) | Multi-layer plastic vessel superior in surface gloss property | |
EP1202914B1 (en) | Transparent multilayer polypropylene container with barrier protection | |
JPH0958648A (en) | Plastic bottle and manufacture thereof | |
JP3536698B2 (en) | Multilayer plastic container | |
JP3702503B2 (en) | Oily food container | |
JP3843687B2 (en) | Lightweight squeeze bottle | |
JP3134376B2 (en) | Multilayer plastic container | |
US20040005475A1 (en) | Transparent multilayer polypropylene container with barrier protection | |
JP3899787B2 (en) | Polypropylene multilayer blow bottle with excellent gloss and impact resistance | |
JP2003182744A (en) | Multilayer blow pack having improved clarity and its production method | |
JP2004237647A (en) | Plastic multi-layer container for oxidizing hair dye | |
JP2643745B2 (en) | Frost-shaped plastic container and method for producing the same | |
JP4622198B2 (en) | Light weight multi-layer plastic container and manufacturing method thereof | |
JP2649619B2 (en) | High gloss multilayer hollow container | |
JPS6049939A (en) | Transparent blow molding vessel and manufacture thereof | |
JP2982274B2 (en) | Frost-like multilayer plastic container and method for producing the same | |
JP3774973B2 (en) | Blow bag and manufacturing method thereof | |
JP4724991B2 (en) | Light weight multi-layer plastic bottle and manufacturing method thereof | |
JPH10286896A (en) | Multilayer vessel with frosted glasslike outward appearance | |
JPH058355A (en) | Multilayered plastic container | |
JPH05111952A (en) | Manufacture of blow plastic vessel having excellent surface gloss | |
AU644708B2 (en) | A frosted container | |
JP2996037B2 (en) | Multilayer plastic container |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |