JPH07108583A - Polyester sheet excellent in heat sealability and molded product thereof - Google Patents
Polyester sheet excellent in heat sealability and molded product thereofInfo
- Publication number
- JPH07108583A JPH07108583A JP5277655A JP27765593A JPH07108583A JP H07108583 A JPH07108583 A JP H07108583A JP 5277655 A JP5277655 A JP 5277655A JP 27765593 A JP27765593 A JP 27765593A JP H07108583 A JPH07108583 A JP H07108583A
- Authority
- JP
- Japan
- Prior art keywords
- molded product
- copolyester
- polyester
- heat
- polyester sheet
- 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
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は改善されたポリエステル
成形品、更に詳しくは、透明性、耐衝撃性を維持しヒー
トシール性が改良されたポリエステル成形品に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improved polyester molded product, and more particularly to a polyester molded product which maintains transparency and impact resistance and has improved heat sealability.
【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)に代表される結晶性ポリ
エステル樹脂は繊維を初めとしてシート、フィルム用ポ
リマーとして広く使用されているが、その優れた耐薬品
性及び低ガス透過性を生かして炭酸飲料、ジュース、ビ
ール等飲料用ボトル、化粧品容器、食品用トレーなどに
も応用される様になってきた。中でもPETより成るシ
ートを熱成形して得られる成形品は食品、食料等の容器
に広く利用されている。2. Description of the Related Art Polyesters, particularly crystalline polyester resins represented by polyethylene terephthalate (hereinafter referred to as PET) are widely used as polymers for sheets and films including fibers, but they have excellent chemical resistance and low resistance. Taking advantage of gas permeability, it has come to be applied to carbonated drinks, juice, bottles for beverages such as beer, cosmetic containers, and food trays. Among them, molded products obtained by thermoforming a sheet made of PET are widely used for containers for foods, foods and the like.
【0003】しかしながら、PETシートによる熱成形
品はヒートシール性に乏しく、圧空成形で低温(90℃
付近)の予熱温度にて成形した物でしかヒートシール出
来ない。特に真空成形品は、完全にはヒートシール出来
ない。However, a thermoformed product made of a PET sheet has poor heat-sealing property, and it is low in pressure molding (90 ° C.).
It can be heat-sealed only with a product molded at the preheating temperature of (near). Especially, vacuum molded products cannot be completely heat-sealed.
【0004】一般に、ポリエステルフィルムのヒートシ
ール性を向上させるためには、PETフィルムに共重合
ポリエステルを積層(ラミネート)させる方法が用いら
れている。Generally, in order to improve the heat-sealing property of a polyester film, a method of laminating a copolymer polyester on a PET film is used.
【0005】しかし、PETシートに共重合ポリエステ
ルを積層(ラミネート)して改善する方法では、シート
製膜行程と更にラミネート行程とが必要となる。又、単
に共重合ポリエステルを単層シートに製膜した場合で
は、耐衝撃性が劣る。However, in the method of improving by laminating the copolyester on the PET sheet, a sheet forming step and a laminating step are required. Also, when the copolyester is simply formed into a single layer sheet, the impact resistance is poor.
【0006】[0006]
【発明が解決しようとする課題】本発明者等は、この様
な従来の問題点を解決するために鋭意検討した結果、本
発明を完成したものであって、その目的とするところ
は、優れたヒートシール性と耐衝撃性、透明性を有する
ポリエステルシートを提供するにある。DISCLOSURE OF THE INVENTION The present inventors have completed the present invention as a result of extensive studies to solve the above-mentioned conventional problems, and the purpose thereof is excellent. Another object is to provide a polyester sheet having heat sealability, impact resistance, and transparency.
【0007】[0007]
【課題を解決するための手段】上述の目的は、芳香族ポ
リエステルと、結晶融解熱が8cal/g以下で280
℃、せん断速度100s-1における溶融粘度が1200
poise以上の共重合ポリエステルとを共押出したこ
とを特徴とする多層ポリエステルシートによって達成さ
れる。[Means for Solving the Problems] The above-mentioned objects are the aromatic polyester and 280 when the heat of fusion of crystal is 8 cal / g or less.
Melt viscosity at ℃, shear rate 100s -1 is 1200
It is achieved by a multilayer polyester sheet characterized by being coextruded with a poise or higher copolyester.
【0008】本発明を構成する第1の要件であるヒート
シール性を有する共重合ポリエステルとは、テレフタル
酸成分の一部をイソフタル酸、2,6−ナフタレンジカ
ルボン酸、アジピン酸、ジフェニルジカルボン酸、ジフ
ェニルエーテルジカルボン酸、ジフェニルスルフォンジ
カルボン酸、セバシン酸等の如き他の1種以上のジカル
ボン酸成分へ置換し使用され得るが、特にイソフタル酸
及び2,6−ナフタレンジカルボン酸が好ましい。エチ
レングリコール成分の一部をジエチレングリコール、ヘ
キサメチレングリコール、トリメチレングリコール、プ
ロピレングリコール、ネオペンチルグリコール、ブチレ
ングリコール、1,4−シクロヘキサンジメタノール等
の如き他の1種以上のグリコール成分で置換した共重合
ポリエステルも使用され得るが、特に1,4−シクロヘ
キサンジメタノールが好ましい。The copolyester having the heat-sealing property which is the first requirement constituting the present invention means that part of the terephthalic acid component is isophthalic acid, 2,6-naphthalenedicarboxylic acid, adipic acid, diphenyldicarboxylic acid, It may be used by substituting it with one or more other dicarboxylic acid components such as diphenyl ether dicarboxylic acid, diphenyl sulfone dicarboxylic acid, sebacic acid and the like, but isophthalic acid and 2,6-naphthalenedicarboxylic acid are particularly preferable. Copolymerization in which a portion of the ethylene glycol component is replaced with one or more other glycol components such as diethylene glycol, hexamethylene glycol, trimethylene glycol, propylene glycol, neopentyl glycol, butylene glycol, 1,4-cyclohexanedimethanol, etc. Polyesters may also be used, but 1,4-cyclohexanedimethanol is particularly preferred.
【0009】本発明に用いる共重合ポリエステルは、結
晶融解熱が8cal/g以下で、280℃、せん断速度
100s-1における溶融粘度が1200poise以上
の物である。結晶融解熱が8cal/gを超える物は、
熱成形時特に真空成形時に表面が微結晶化してしまいヒ
ートシール性が悪化する。又280℃の溶融粘度が12
00poise未満の物は、共押出シート製膜時に隣層
との溶融粘度の差が大きくなりフローマークが発生し綺
麗なシートは得られない。The copolyester used in the present invention has a heat of crystal fusion of 8 cal / g or less and a melt viscosity of 1200 poise or more at 280 ° C. and a shear rate of 100 s -1 . Those whose heat of crystal fusion exceeds 8 cal / g are
At the time of thermoforming, especially at the time of vacuum forming, the surface is crystallized to deteriorate the heat sealability. The melt viscosity at 280 ° C is 12
If the porosity is less than 00 poise, the difference in melt viscosity between the co-extruded sheet and the adjacent layer becomes large and flow marks are generated, so that a clean sheet cannot be obtained.
【0010】共重合ポリエステルの酸成分の一部にイソ
フタル酸を使用する場合、エチレンテレフタレートに対
して8〜15mol%共重合した物が、ヒートシール
性、耐衝撃性の点から好ましい。When isophthalic acid is used as a part of the acid component of the copolymerized polyester, a copolymerized product of 8 to 15 mol% with respect to ethylene terephthalate is preferable from the viewpoint of heat sealability and impact resistance.
【0011】共重合ポリエステルのグリコール成分の一
部に1,4−シクロヘキサンジメタノールを使用する場
合、エチレンテレフタレートに対して5〜35mol%
共重合した物がヒートシール性、粘度アップの点で好ま
しい。When 1,4-cyclohexanedimethanol is used as a part of the glycol component of the copolyester, it is 5 to 35 mol% with respect to ethylene terephthalate.
A copolymerized product is preferable in terms of heat sealability and viscosity increase.
【0012】共重合ポリエステルの酸成分の一部に2,
6−ナフタレンジカルボン酸を使用する場合、エチレン
テレフタレートに対して5〜35mol%共重合した物
がヒートシール性、粘度アップの点で好ましい。Some of the acid component of the copolyester is 2,
When 6-naphthalenedicarboxylic acid is used, a copolymer of 5 to 35 mol% with respect to ethylene terephthalate is preferable in terms of heat sealability and viscosity increase.
【0013】本発明を構成する第2の要件である芳香族
ポリエステルとは、ポリエチレンテレフタレート、ポリ
エチレンナフタレートは勿論のこと、それらの性質を変
えない範囲内でテレフタル酸成分の一部をイソフタル
酸、アジピン酸、ジフェニルジカルボン酸、ジフェニル
エーテルジカルボン酸、ジフェニルスルフォンジカルボ
ン酸、セバシン酸、ナフタレンジカルボン酸等の如き他
の1種以上のジカルボン酸成分へ置換し、エチレングリ
コール成分の一部をジエチレングリコール、ヘキサメチ
レングリコール、トリメチレングリコール、プロピレン
グリコール、1,4−シクロヘキサンジメタノール、ネ
オペンチルグリコール、ブチレングリコール等の如き他
の1種以上のグリコール成分で置換したものでもよい。
ポリエステルの固有粘度は、20℃に於ける重量比60
/40のフェノール/テトラクロロエタン混合溶媒中で
の測定において、約0.5〜1.2が熱成形後の製品と
しての機械的強度、又熱成形の点で好ましく、更に好ま
しくは0.6以上である。The aromatic polyester which is the second requirement constituting the present invention means not only polyethylene terephthalate and polyethylene naphthalate but also a part of the terephthalic acid component is isophthalic acid within a range that does not change the properties thereof. Substituting one or more other dicarboxylic acid components such as adipic acid, diphenyldicarboxylic acid, diphenyletherdicarboxylic acid, diphenylsulfonedicarboxylic acid, sebacic acid, naphthalenedicarboxylic acid, etc., and replacing a part of the ethylene glycol component with diethylene glycol, hexamethylene glycol , Trimethylene glycol, propylene glycol, 1,4-cyclohexanedimethanol, neopentyl glycol, butylene glycol, etc., may be substituted with one or more other glycol components.
The intrinsic viscosity of polyester is 60 at a weight ratio at 20 ° C.
/ 40 in a phenol / tetrachloroethane mixed solvent, about 0.5 to 1.2 is preferable in terms of mechanical strength as a product after thermoforming and thermoforming, and more preferably 0.6 or more. Is.
【0014】本発明の樹脂組成物には、ポリマーの本質
的な性質を変えない範囲内で添加剤、帯電防止剤、紫外
線吸収剤、安定剤、及びカーボンブラック、タルク、マ
イカ、二酸化チタン、炭酸カルシウム、アルミナ、シリ
カ、ワラストナイト、カオリン等の無機粒子や顔料を含
有する事ができる。In the resin composition of the present invention, additives, antistatic agents, ultraviolet absorbers, stabilizers, carbon black, talc, mica, titanium dioxide, carbonic acid are added within a range that does not change the essential properties of the polymer. Inorganic particles and pigments such as calcium, alumina, silica, wollastonite and kaolin may be contained.
【0015】本発明の多層ポリエステルシートの厚さは
通常0.15〜1mmが容器の剛性、工業生産性の点で
好ましい。このシートを加工して得られる容器は箇所に
よって若干厚さが異なるが、延伸部以外、通常はシート
の厚さとさして異ならないものとする。The thickness of the multilayer polyester sheet of the present invention is preferably 0.15 to 1 mm, from the viewpoints of container rigidity and industrial productivity. The container obtained by processing this sheet has a slightly different thickness depending on the location, but normally, except for the stretched portion, it does not differ from the thickness of the sheet.
【0016】又、芳香族ポリエステルが、共重合ポリエ
ステルの厚みの4〜30倍である熱成形品が容器の強
度、ヒートシール性強度の点で好ましい。Further, a thermoformed product in which the aromatic polyester is 4 to 30 times the thickness of the copolyester is preferable from the viewpoint of container strength and heat sealability.
【0017】次に該樹脂組成物を押出機により溶融押出
後、急冷し、無延伸で結晶化度3%以下の非晶質の上記
厚みのシートを製造し、容器に製造する。成形手段とし
ては、真空成形、圧空成形、スナップバック成形、レバ
ースドロー成形、エアースリップ成形、プラグアシスト
成形、熱盤成形またはこれらを組み合わせた成形方法が
常法として知られているが、本発明ではいずれの方法を
用いても差し支えない。Next, the resin composition is melt-extruded by an extruder and then rapidly cooled, and an amorphous sheet having a crystallinity of 3% or less and having the above-mentioned thickness is produced without stretching, and is produced in a container. As the molding means, vacuum molding, pressure molding, snapback molding, lever draw molding, air slip molding, plug assist molding, hot plate molding or a molding method combining these is known as a conventional method. Then, either method can be used.
【0018】又、成形品が絞り比(間口に対する深さ)
0.1〜1.5の容器本体である方が容積確保、成形性
の点で好ましい。Further, the molded product has a drawing ratio (depth with respect to the frontage).
A container body having a volume of 0.1 to 1.5 is preferable in terms of securing volume and moldability.
【0019】[0019]
【発明の効果】本発明の成形品は、ヒートシール性要求
側の表面にヒートシール性を有する結晶融解熱が8ca
l/g以下で、280℃の溶融粘度が1200pois
e以上の共重合ポリエステルを芳香族ポリエステルと共
押出しして使用しているため、ヒートシール性、印刷
性、ガス透過性、機械物性に優れており、また、着香成
分の吸着が少ないため、食品容器、薬品容器等に最適で
ある。又、特に真空成形品のヒートシール性も優れる
為、幅広い熱成形機に対応可能である。EFFECTS OF THE INVENTION The molded product of the present invention has a heat of crystal fusion having a heat sealability of 8 ca on the surface on the heat sealability required side.
Melt viscosity at 280 ° C is 1200 pois at 1 / g or less
Since the copolyester of e or more is co-extruded with the aromatic polyester and used, it has excellent heat sealability, printability, gas permeability, and mechanical properties, and also has little adsorption of flavor components, Most suitable for food containers, chemical containers, etc. Further, since the heat-sealing property of the vacuum-formed product is particularly excellent, it can be applied to a wide range of thermoforming machines.
【0020】[0020]
【実施例】以下、実施例によって本発明を更に具体的に
説明するが、本発明はこれに限定されるものではない。The present invention will be described in more detail with reference to the following examples, but the present invention is not limited thereto.
【0021】実施例1〜4、比較例1〜2 表1に示すPETペレットを水分率0.01%以下にな
るように乾燥し、Tダイを設けた多層押出機により厚さ
0.5mmのシートを得、該シートを45℃に温調した
雌金型を取り付けた真空熱成形機によって縦157mm
×横110mm×深さ34mm(最大絞り比0.31)
の容器を作成し、下記の事項について試験を行った。結
果を表1に示す。Examples 1 to 4 and Comparative Examples 1 to 2 The PET pellets shown in Table 1 were dried to a water content of 0.01% or less, and a 0.5 mm-thick film was formed with a multi-layer extruder equipped with a T-die. A sheet was obtained, and the length was 157 mm by a vacuum thermoforming machine equipped with a female mold whose temperature was controlled at 45 ° C.
× width 110 mm × depth 34 mm (maximum drawing ratio 0.31)
The container was prepared and the following items were tested. The results are shown in Table 1.
【0022】1.ヒートシール性;厚さ0.22mmの
蓋材(PET)と該容器を温度190℃、時間2秒、圧
力2.5kg/cm2 でヒートシールさせ剥離強度を測
定した。サンプルの剥離幅は、15mmである。(目標
値1000g/15mm以上) 2.衝撃強度;東洋精機(株)グラフィックインパクト
テスターにてシートの衝撃強度測定した。シート厚み5
00ミクロンで、亀裂発生エネルギーが3.5〜4Jが
好ましい。 3.低温衝撃強度;容器に水200gを入れ、上記条件
でヒートシールした容器を−30℃で24時間放置後、
コンクリート床面に容器の側部を下にして落下させ、5
0%破壊時の高さを測定、60cm未満を×、60〜1
00cmを△、100cm以上を○とした。 4.シート製膜性;シート製膜時目視で判断した。きれ
いに製膜出来ていたら○、フローマーク等が出たら×。1. Heat-sealing property: The lid material (PET) having a thickness of 0.22 mm and the container were heat-sealed at a temperature of 190 ° C. for 2 seconds and a pressure of 2.5 kg / cm 2 to measure the peel strength. The peel width of the sample is 15 mm. (Target value 1000 g / 15 mm or more) 1. Impact strength: The impact strength of the sheet was measured by Toyo Seiki Co., Ltd. Graphic Impact Tester. Sheet thickness 5
It is preferable that the crack initiation energy is 3.5 to 4 J at 00 microns. 3. Low temperature impact strength; 200 g of water was placed in a container, and the container heat-sealed under the above conditions was left at -30 ° C for 24 hours,
Drop it on the concrete floor with the side of the container down and
Measure the height at 0% destruction, x less than 60 cm, 60 to 1
00 cm was evaluated as Δ and 100 cm or more was evaluated as ◯. 4. Sheet film-forming property: Judgment was visually performed at the time of sheet film formation. ○ if the film was formed cleanly, and × if a flow mark etc. appeared.
【0023】[0023]
【表1】 [Table 1]
【0024】CHDM;シクロヘキサンジメタノール NDCA;ナフタレンジカルボン酸CHDM; cyclohexanedimethanol NDCA; naphthalenedicarboxylic acid
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29L 9:00 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location B29L 9:00
Claims (7)
cal/g以下で280℃、せん断速度100s-1にお
ける溶融粘度が1200poise以上の共重合ポリエ
ステルとを共押出したことを特徴とする多層ポリエステ
ルシート。1. An aromatic polyester having a heat of fusion of crystal of 8
A multilayer polyester sheet characterized by being coextruded with a copolyester having a melt viscosity of 1200 poise or more at 280 ° C. at a cal / g or less and a shear rate of 100 s −1 .
からなる成形品。2. A molded product comprising the multilayer polyester sheet according to claim 1.
チレンテレフタレートに対して8〜15mol%共重合
したものである請求項2記載の成形品。3. The molded article according to claim 2, wherein the copolyester is obtained by copolymerizing isophthalic acid with ethylene terephthalate in an amount of 8 to 15 mol%.
キサンジメタノール又は2,6−ナフタレンジカルボン
酸をエチレンテレフタレートに対して5〜35mol%
共重合したものである請求項2記載の成形品。4. The copolymerized polyester comprises 1,4-cyclohexanedimethanol or 2,6-naphthalenedicarboxylic acid in an amount of 5 to 35 mol% based on ethylene terephthalate.
The molded article according to claim 2, which is a copolymer.
の成形品。5. The molded article according to claim 2, wherein the molded article is a main body of a container.
エステルの厚みの4〜30倍である請求項2記載の成形
品。6. The molded product according to claim 2, wherein the thickness of the aromatic polyester is 4 to 30 times the thickness of the copolyester.
記載の成形品。7. The drawing ratio is 0.1 to 1.5.
Molded product described.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27765593A JP3229463B2 (en) | 1993-10-07 | 1993-10-07 | Polyester sheet excellent in heat sealability and molded product thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27765593A JP3229463B2 (en) | 1993-10-07 | 1993-10-07 | Polyester sheet excellent in heat sealability and molded product thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07108583A true JPH07108583A (en) | 1995-04-25 |
JP3229463B2 JP3229463B2 (en) | 2001-11-19 |
Family
ID=17586460
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27765593A Expired - Fee Related JP3229463B2 (en) | 1993-10-07 | 1993-10-07 | Polyester sheet excellent in heat sealability and molded product thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3229463B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10315417A (en) * | 1997-05-20 | 1998-12-02 | Mitsubishi Chem Corp | Laminated polyester sheet |
KR19990040652A (en) * | 1997-11-19 | 1999-06-05 | 구광시 | Transparency Copolyester Plate Sheet |
KR100534515B1 (en) * | 1997-12-26 | 2006-03-22 | 주식회사 코오롱 | Transparency Copolyester Plate |
KR100564059B1 (en) * | 1996-12-20 | 2006-07-14 | 훽스트 디아포일 게엠베하 | Co-compressed hot-sealing biaxially oriented polyester film and method for manufacturing same |
WO2014046277A1 (en) * | 2012-09-21 | 2014-03-27 | 東洋製罐株式会社 | Packaging material and packaging structure made by using same |
-
1993
- 1993-10-07 JP JP27765593A patent/JP3229463B2/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100564059B1 (en) * | 1996-12-20 | 2006-07-14 | 훽스트 디아포일 게엠베하 | Co-compressed hot-sealing biaxially oriented polyester film and method for manufacturing same |
JPH10315417A (en) * | 1997-05-20 | 1998-12-02 | Mitsubishi Chem Corp | Laminated polyester sheet |
KR19990040652A (en) * | 1997-11-19 | 1999-06-05 | 구광시 | Transparency Copolyester Plate Sheet |
KR100534515B1 (en) * | 1997-12-26 | 2006-03-22 | 주식회사 코오롱 | Transparency Copolyester Plate |
WO2014046277A1 (en) * | 2012-09-21 | 2014-03-27 | 東洋製罐株式会社 | Packaging material and packaging structure made by using same |
JP2014061663A (en) * | 2012-09-21 | 2014-04-10 | Toyo Seikan Kaisha Ltd | Packaging material and packaging structure using the same |
US11407212B2 (en) | 2012-09-21 | 2022-08-09 | Toyo Seikan Group Holdings, Ltd. | Packaging material and packaging structure made by using same |
Also Published As
Publication number | Publication date |
---|---|
JP3229463B2 (en) | 2001-11-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7205040B2 (en) | Peelable polyester film having improved oxygen barrier, process for its production and its use | |
US7141293B2 (en) | Coextruded, hot-sealable and peelable polyester film having high peeling resistance, process for its production and its use | |
US7144615B2 (en) | Coextruded, hot-sealable and peelable polyester film, process for its production and its use | |
US20050019559A1 (en) | Coextruded, hotsealable and peelable polyester film having easy peelability, process for its production and its use | |
US20050121822A1 (en) | Process for producing a coextruded, peelable polyester film | |
KR20090078348A (en) | Heat-sealable composite polyester film | |
US7288312B2 (en) | Coextruded, hot-sealable and peelable polyester film having low peeling resistance, process for its production and its use | |
AU764519B2 (en) | Multi layered thermoplastic container | |
US20050074599A1 (en) | Coextruded, hot-sealable and peelable polyester film, process for its production and its use | |
JPH09254346A (en) | Multilayered polyester sheet and packaging container produced by working it | |
US20040213968A1 (en) | Coextruded, heatsealable and peelable polyester film, process for its production and its use | |
JP2000141575A (en) | Laminated film comprising oxygen gas high barrier biaxially-oriented polyester film and production and use thereof | |
US7223459B2 (en) | Coextruded, hot-sealable and peelable polyester film, process for its production and its use | |
US20200079064A1 (en) | Heat-sealable polyester film for production of ready-meal trays, process for its production, and use of the film | |
JP3229463B2 (en) | Polyester sheet excellent in heat sealability and molded product thereof | |
US20190389187A1 (en) | Thermoformable transparent packing made of polyester with a lower foil and an upper foil, process for production thereof and use thereof | |
JPH09272191A (en) | Multilayered polyester sheet and container consisting of it | |
JPH08267686A (en) | Heat forming polyester sheet and formed item thereof | |
US20200223607A1 (en) | Pack made of polyester with a thermoformable lower film and a sealable and peelable upper film, use thereof, and process for its production | |
JPH0952338A (en) | Polyester sheet and container having high impact resistance | |
JPH08156210A (en) | Thermoformed polyester container excellent in slip properties | |
JP3329606B2 (en) | Polyester sheet excellent in slipperiness and molded product thereof | |
JP3464531B2 (en) | Deep drawn thermoformed polyester container | |
JPH01289826A (en) | Polyester molding | |
JPH081767A (en) | Polyester vessel with excellent impact resistance |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313113 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20070907 Year of fee payment: 6 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080907 Year of fee payment: 7 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080907 Year of fee payment: 7 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090907 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090907 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100907 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110907 Year of fee payment: 10 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120907 Year of fee payment: 11 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130907 Year of fee payment: 12 |
|
LAPS | Cancellation because of no payment of annual fees |