JPS62231720A - Polyester vessel and its manufacture - Google Patents
Polyester vessel and its manufactureInfo
- Publication number
- JPS62231720A JPS62231720A JP61072442A JP7244286A JPS62231720A JP S62231720 A JPS62231720 A JP S62231720A JP 61072442 A JP61072442 A JP 61072442A JP 7244286 A JP7244286 A JP 7244286A JP S62231720 A JPS62231720 A JP S62231720A
- Authority
- JP
- Japan
- Prior art keywords
- polyester
- container
- temperature
- vessel
- crystallinity
- 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
- 229920000728 polyester Polymers 0.000 title claims abstract description 49
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000000463 material Substances 0.000 claims abstract description 20
- -1 polyethylene terephthalate Polymers 0.000 claims abstract description 19
- 238000001816 cooling Methods 0.000 claims abstract description 18
- 229920000139 polyethylene terephthalate Polymers 0.000 claims abstract description 16
- 239000005020 polyethylene terephthalate Substances 0.000 claims abstract description 16
- 238000000465 moulding Methods 0.000 claims abstract description 8
- 230000009477 glass transition Effects 0.000 claims abstract description 5
- 238000002425 crystallisation Methods 0.000 claims description 15
- 230000008025 crystallization Effects 0.000 claims description 15
- 238000003856 thermoforming Methods 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 10
- 238000010438 heat treatment Methods 0.000 abstract description 4
- 230000002349 favourable effect Effects 0.000 abstract 1
- 239000004615 ingredient Substances 0.000 abstract 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 11
- 239000002253 acid Substances 0.000 description 9
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 6
- 230000001070 adhesive effect Effects 0.000 description 5
- 239000000853 adhesive Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 4
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical group OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 238000007666 vacuum forming Methods 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
- 229920001634 Copolyester Polymers 0.000 description 2
- 239000004743 Polypropylene 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
- 230000007547 defect Effects 0.000 description 2
- 238000001739 density measurement Methods 0.000 description 2
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 2
- KZTYYGOKRVBIMI-UHFFFAOYSA-N diphenyl sulfone Chemical compound C=1C=CC=CC=1S(=O)(=O)C1=CC=CC=C1 KZTYYGOKRVBIMI-UHFFFAOYSA-N 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 230000000977 initiatory effect Effects 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000000454 talc Substances 0.000 description 2
- 229910052623 talc Inorganic materials 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- HZNVPDKRGZKQAW-UHFFFAOYSA-N 2-[1,1-bis[4-(2-hydroxyethoxy)phenyl]ethyl]propane-1,3-diol Chemical compound C(O)C(C(C)(C1=CC=C(C=C1)OCCO)C1=CC=C(C=C1)OCCO)CO HZNVPDKRGZKQAW-UHFFFAOYSA-N 0.000 description 1
- XCSGHNKDXGYELG-UHFFFAOYSA-N 2-phenoxyethoxybenzene Chemical compound C=1C=CC=CC=1OCCOC1=CC=CC=C1 XCSGHNKDXGYELG-UHFFFAOYSA-N 0.000 description 1
- QLIQIXIBZLTPGQ-UHFFFAOYSA-N 4-(2-hydroxyethoxy)benzoic acid Chemical compound OCCOC1=CC=C(C(O)=O)C=C1 QLIQIXIBZLTPGQ-UHFFFAOYSA-N 0.000 description 1
- 241000473391 Archosargus rhomboidalis Species 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 125000006267 biphenyl group Chemical group 0.000 description 1
- 238000007707 calorimetry Methods 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- FOTKYAAJKYLFFN-UHFFFAOYSA-N decane-1,10-diol Chemical compound OCCCCCCCCCCO FOTKYAAJKYLFFN-UHFFFAOYSA-N 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002156 mixing Methods 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
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 150000003457 sulfones Chemical class 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C66/00—General aspects of processes or apparatus for joining preformed parts
- B29C66/70—General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material
- B29C66/71—General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material characterised by the composition of the plastics material of the parts to be joined
Landscapes
- Containers Having Bodies Formed In One Piece (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
- Lining Or Joining Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はポリエステル容器及びその製造法に関し、史に
詳しくは、例えばオープンWA理可能(以下、オーブチ
プルということがある)な耐熱変形性の優れた容器であ
って、かつ蓋材を容易に熱接着することが6J能なポリ
エステル容器及びその製造法に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a polyester container and a method for manufacturing the same. The present invention relates to a polyester container which can be easily heat-bonded with a lid material, and a method for manufacturing the same.
ポリエステル、特にポリエチレンテレフタレートより成
るシートを熱成形して得られる成形体は食品9食料等の
容器として広く使用されておシ、特に近年例えば特開昭
59−62660号公報に記載の如く、結n性を尚める
ことにょシ耐熱変形+11を改良せしめたポリエステル
熟成形体はオーブナブルトレイとして使用されるに至っ
ている。このポリエステル容器は通常ポリエチレンテレ
フタレートが結晶化可能な一度条件の高温金型を用いて
ポリエチレンテレフタレートシートを熱成形することに
よシ侍られる。Molded bodies obtained by thermoforming sheets made of polyester, particularly polyethylene terephthalate, are widely used as containers for foodstuffs, etc. In recent years, as described in JP-A-59-62660, for example, molded bodies have been widely used as containers for foods. Aged polyester molds with improved heat resistance and deformation +11 have come to be used as ovenable trays. The polyester container is typically prepared by thermoforming a polyethylene terephthalate sheet using a one-time high temperature mold in which the polyethylene terephthalate can crystallize.
しかしながら、この方法で得たポリエステル容器は、ポ
リエステルが結晶化しているため、通常の蓋材との熱接
着性が低く、特にレトルト殺菌等の高温11処理をhし
ても接着力を保つことは困難であるという欠点を有して
いるので、その教養が望まれている。However, the polyester containers obtained by this method have low thermal adhesion to ordinary lid materials because the polyester is crystallized, and in particular, they do not maintain adhesive strength even after hours of high-temperature treatment such as retort sterilization. Since it has the disadvantage of being difficult, its education is desired.
本発明は、このような問題点を解決しようとしてなされ
たものであり、その目的は優れた耐熱性を有し、かつ蓋
材との接着性の良好なポリエステル容器とその8器を効
率良く成形する方法を提供することに、Sる。The present invention was made to solve these problems, and its purpose is to efficiently mold a polyester container that has excellent heat resistance and good adhesion to the lid material, and 8 containers thereof. Our aim is to provide a method to do so.
本発明者は、+iff記の如き欠点のないポリエステル
容器及びその成形法に関し鋭芭研究の結果、ポリエステ
ルシートを特定の結晶化度となるよう加熱せしめた後、
特定温度に保った状態の金型を用いて熱成形することに
より欠点を改善し得ることを見出し本発明に到達した1
゜即ち、本発明は、
(1) ポリエチレンテレフタレートを主たる構成成
分とするポリエステル製シートを熱成形して得られる容
器であって、該容器における蓋材との熱接着部分の結晶
化度が20%未満であシ、該容部の底部及び/又は側部
の結晶化度が20−以上であることを特徴とするポリエ
ステル容器及び
(2) ポリエチレンテレフタレートを主たる構成成
分とする実質的に非晶なポリエステル製シートを結晶化
度が20%未満の状態で加熱軟化せしめたのち、該ポリ
エステルの結晶化温度範囲に保っである金型により熱成
形してポリエステル製容器を製造するに際し、核芥器に
おける蓋材との熱接着部分に該ポリエステルのガラス転
位温度+20℃以下の温度範囲に保っである冷却用部材
を接触せしめることからなるポリエステル容器の製造法
である。As a result of intensive research into a polyester container and its molding method that do not have the drawbacks described above, the inventor has discovered that after heating a polyester sheet to a specific degree of crystallinity,
The present invention was achieved by discovering that the defects could be improved by thermoforming using a mold kept at a specific temperature.
That is, the present invention provides: (1) a container obtained by thermoforming a polyester sheet containing polyethylene terephthalate as a main component, wherein the degree of crystallinity of the part of the container that is thermally bonded to the lid material is 20%; (2) a polyester container characterized in that the degree of crystallinity of the bottom and/or sides of the container is not less than 20, and (2) a substantially amorphous container whose main constituent is polyethylene terephthalate; When producing a polyester container by heating and softening a polyester sheet with a crystallinity of less than 20% and then thermoforming it in a mold that is kept within the crystallization temperature range of the polyester, This is a method for producing a polyester container, which comprises bringing a cooling member, which is maintained at a temperature within the glass transition temperature of the polyester +20° C., into contact with the thermally bonded portion with the lid material.
本発明(1)について説明すると、
本発明においてポリエチレンテレフタレートは、そのホ
モポリマーは勿論のこと、テレフタルば成分の一部又は
グリコール成分の一部を他の酸又はグリコールで置換し
たものを包含する。To explain the present invention (1), polyethylene terephthalate in the present invention includes not only homopolymers thereof but also those in which a part of the terephthalic component or a part of the glycol component is replaced with another acid or glycol.
例えば、酸成分の一部をイソフタル酸、ナフタリンジカ
ルボ7市、ジフェニルジ力ルボ/酸。For example, part of the acid component is isophthalic acid, naphthalene dicarboxylic acid, diphenyl dicarbohydrate/acid.
ジフェノキシエタンジカルボン酸、ジフェニルエーテル
ジカルボン酸、ジフェニルスルホンジカルボン酸等の如
き芳香族ジカルボ/酸;ヘキサヒドロテレフタル91ヘ
キナヒドロイソフタルrR等の如き脂環族ジカルボン酸
;アジピン酸。Aromatic dicarboxylic acids such as diphenoxyethane dicarboxylic acid, diphenyl ether dicarboxylic acid, diphenylsulfone dicarboxylic acid, etc.; alicyclic dicarboxylic acids such as hexahydroterephthal 91 hequinahydroisophthal rR; adipic acid.
セパチン酸、アぜ′ライン酸等の如き脂肪族ジカルボン
酸;p−β−ヒドロキシエトキシ安息香酸、p−オキシ
安息香酸、ε−オキシカプロン酸等の如きオキシ酸等の
他の二官能性カルボン酸のIMi以上の成分で置換した
ものが挙けられる。更に1工チレングリコール成分の一
部を例えばトリメチレングリコール、テトラメチレング
リコール、ヘキサメチレングリコール、デカメチレング
リコール、ネオベンテレンクリコール、ジエチレングリ
コール、1.1−シクロヘキサンジメチロール、1.4
−シクロヘキサンジメチロール、2.2−ビス(4−β
−ヒドロキシエトキシフェニル)プロパン、ビス(4−
β−ヒドロキシエトキシフェニル)スルホン等の他のグ
リコールのla!以上の成分で置換したコポリエステル
をも包含する。これらのコポリエステル甲の共重合成分
CI Nm W1合は全酸成分に対し3モルチ以下であ
ることが好ましい。これらのうちポリエチレンテレフタ
レートのホモポリマーが好ましい。Aliphatic dicarboxylic acids such as cepacic acid, azillaic acid, etc.; other difunctional carboxylic acids such as oxyacids such as p-β-hydroxyethoxybenzoic acid, p-oxybenzoic acid, ε-oxycaproic acid, etc. Examples include those substituted with a component greater than or equal to IMi. Further, a part of the 1-functional ethylene glycol component may be added to, for example, trimethylene glycol, tetramethylene glycol, hexamethylene glycol, decamethylene glycol, neoventerene glycol, diethylene glycol, 1.1-cyclohexane dimethylol, 1.4
-cyclohexane dimethylol, 2,2-bis(4-β
-hydroxyethoxyphenyl)propane, bis(4-
of other glycols such as β-hydroxyethoxyphenyl) sulfone! Copolyesters substituted with the above components are also included. The copolymerization component CI Nm W1 of these copolyesters A is preferably 3 molar or less based on the total acid components. Among these, a homopolymer of polyethylene terephthalate is preferred.
本発明に用いるポリエステルシートとは、ポリエチレン
テレフタレートを主たる構成4分とする実質的に非晶質
のシートであり、その固有粘度は0.8以上であること
が好ましい。ポリエステルシートには、結晶化促進効果
のある添加剤又は離型ハIIを含んでいてもよく、更&
てボリエチレン(以下PEと記すことあり)、ポリプロ
ピレン(以下PPと記すことあり)を1〜30重量%混
合せしめたシートであっても良い。このポリエステルシ
ートはPETの結晶化度が20チ未満のものを用いるが
、ここでいう結晶化度とは、(11〜(31式により求
められた数値である。The polyester sheet used in the present invention is a substantially amorphous sheet mainly composed of polyethylene terephthalate, and preferably has an intrinsic viscosity of 0.8 or more. The polyester sheet may contain additives or mold release II that have the effect of promoting crystallization, and
It may also be a sheet in which polyethylene (hereinafter sometimes referred to as PE) and polypropylene (hereinafter sometimes referred to as PP) are mixed in an amount of 1 to 30% by weight. This polyester sheet uses PET having a crystallinity of less than 20 inches, and the crystallinity here is a numerical value determined by formulas (11 to (31).
ρo = 1.333− (Wx 0.0040 )−
−−”・・(1)ρc=1.455−(WXo、005
3)−−=−・・・ f2)C=((ρ−ρ0)/(ρ
C−ρo ) l X 100−−−−−−−−・(3
1P1uTの結晶化度が20%以上のシートであると熱
成形の際の賦型性が悪く、また蓋材との熱接着性が不良
となる。ρo = 1.333- (Wx 0.0040)-
--”...(1) ρc=1.455-(WXo, 005
3)--=-... f2) C=((ρ-ρ0)/(ρ
C-ρo) l
If the crystallinity of 1P1uT is 20% or more, the shapeability during thermoforming will be poor, and the thermal adhesion to the lid material will be poor.
本発明(2)では、ポリエステルシートを結晶化度が2
0%未満の状態で加熱軟化せしめて熱成形するが、結晶
化度をこの状態に保つにはシートの加熱時間15秒以内
でシート表面温度140℃以上に加熱することが好まし
い。上記時間を超えるとPETの結晶化誘導期を過ぎる
ため、シート中のPET分が急速に結晶化する現象が起
き、結果として賦型性が悪くなシ、好ましくない。In the present invention (2), the polyester sheet has a crystallinity of 2
The sheet is softened and thermoformed in a state of less than 0%, but in order to maintain the crystallinity in this state, it is preferable to heat the sheet to a surface temperature of 140° C. or higher within 15 seconds. If the above-mentioned time is exceeded, the crystallization induction period of PET is passed, and a phenomenon occurs in which the PET portion in the sheet rapidly crystallizes, resulting in poor shaping properties, which is not preferable.
更に、本発明では金型温度をポリエステルの結晶化温度
範囲即ち、水差熱量針(DSc)にて、サンプルを20
℃/−の速度で昇温及び降温せしめた際のポリエステル
の昇温時給晶化開始温度(ToI)以上、降温時結晶化
開始温度(T’co )以下の温度に保っである金型に
より熱成形せしめてポリエステル容器を製造するが、こ
の際に、容器における蓋材との熱接着部分に、該ポリエ
ステルのガラス転位温度(TV ) + 20℃以下の
(特に好ましくはTf以下の)fm度範囲に保っである
冷却用部材を接触せしめる工程を必須とするものである
。Furthermore, in the present invention, the mold temperature is set within the crystallization temperature range of polyester, that is, using a differential calorimetry needle (DSc), and the sample is
When the temperature is raised and lowered at a rate of ℃/-, the polyester is heated by a mold that is maintained at a temperature higher than the crystallization initiation temperature (ToI) and lower than the crystallization initiation temperature (T'co) when the temperature is lowered. A polyester container is manufactured by molding, and at this time, the glass transition temperature (TV) of the polyester is in the fm degree range below +20°C (particularly preferably below Tf) at the thermally bonded part with the lid material of the container. This requires a step of bringing the cooling member into contact with the cooling member.
この冷却用部材の温度がTt+20℃よシも高温If
Kなると1部材と容器との離型が悪くなり、特にT。I
よりも高温になると容器部の結晶化度が高くなるため、
本発明の効果が損われる。If the temperature of this cooling member is higher than Tt+20℃
When the temperature is K, the mold release between one member and the container becomes difficult, especially when the temperature is T. I
When the temperature is higher than that, the crystallinity of the container increases, so
The effect of the present invention is impaired.
また金型温度が前記ポリエステルの結晶化温度範囲をは
ずれると、容器の底部及び/又は側部の結晶化度が不足
して容器の耐熱性がイ9られず、或いは熱成形直後の容
器の収縮が大きくなる。Furthermore, if the mold temperature is out of the crystallization temperature range of the polyester, the crystallinity of the bottom and/or side portions of the container may be insufficient and the heat resistance of the container may not be improved, or the container may shrink immediately after thermoforming. becomes larger.
以上述べた熱成形法により、容器における蓋材との熱接
着部の結晶化度が20チ未満、好ましくは10チ以下で
あり、この容器の底部及び/又は側部の結晶化Ifが2
0係以上、好ましくは30嘔以上のポリエステル容器が
得られる。By the thermoforming method described above, the degree of crystallinity of the thermally bonded part with the lid of the container is less than 20 inches, preferably less than 10 degrees, and the crystallization If of the bottom and/or side part of this container is 2.
A polyester container with a coefficient of 0 or more, preferably 30 or more is obtained.
本発明ではかかるポリエステルシートを特定の条件で熱
成形して、トレイ、カップ等の形状の耐熱性及び熱接着
性の優れた容器を得るが、本発明でいう熱成形とけ、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
の間隙にある空気を排除し、大気圧(0型に密着せしめ
成形する真空成形、或いは大気以上の圧縮空気によシシ
ートを型に密着せしめる圧空成形及び真空、圧空を併用
する成形等を総称する。In the present invention, such polyester sheets are thermoformed under specific conditions to obtain containers with excellent heat resistance and heat adhesive properties in the shape of trays, cups, etc. Press the sheet against the desired mold, eliminate the air in the gap between the mold and the material, and press the sheet into close contact with the mold under atmospheric pressure (vacuum forming), or pressurize the sheet with compressed air above atmospheric pressure and press it against the mold. A general term for molding that uses both vacuum and compressed air.
本発明の熱成形方法により得られるポリエステル成形体
は所望の形状・寸法を有し、耐熱変形性及び蓋材との熱
接着性に優れ、オーブナブルトレイ等として有利に使用
できる。The polyester molded article obtained by the thermoforming method of the present invention has a desired shape and dimensions, has excellent heat deformation resistance and thermal adhesion to a lid material, and can be advantageously used as an ovenable tray or the like.
以下実施例によシ本発明を詳述する。 The present invention will be explained in detail below with reference to Examples.
なお、主な物性値の測定条件および成形体の粁価基準は
次の通シである。The measurement conditions for the main physical property values and the molding value standard are as follows.
(1) η14r粘x [IV) : 0−クロロフ
ェノール又はフェノール/テトラクロルエタン混合酢媒
中で35℃忙て測定。(1) η14r viscosity x [IV]: Measured at 35°C in 0-chlorophenol or phenol/tetrachloroethane mixed vinegar medium.
(2) 密 度〔ρ〕 :四塩化炭素とn−へブタ
ンによシ作成した密度勾配管によシ25℃にて測定。(2) Density [ρ]: Measured at 25°C in a density gradient tube made of carbon tetrachloride and n-hebutane.
(3) ガラス転位温度J1〕:示差熱#:、計(セ
イコー電子工菜株式会社″11!ID S C−20r
法)により20℃/鯛の昇温速度で測定。(3) Glass transition temperature J1]: Differential heat #:, meter (Seiko Electronics Co., Ltd. "11! ID S C-20r
Measured at a heating rate of 20°C/sea bream using the method).
(4) 昇温時給晶化開始温度〔Ta工):Trと同
様の条件で測定。(4) Temperature at which temperature increases during crystallization (Ta process): Measured under the same conditions as Tr.
(5) 融点(ポリエステル) (’rmE) :
Tyと同様の条件で測定。(5) Melting point (polyester) ('rmE):
Measured under the same conditions as Ty.
(6) 降温時結晶化開始温度〔ToD〕:示差pA
irtにて290℃で3分間保持したテンプルを20℃
/悶の降温速度で測定。(6) Crystallization onset temperature upon cooling [ToD]: differential pA
The temple was held at 290℃ for 3 minutes at 20℃.
/Measured by the rate of temperature drop in agony.
(7)融点(ボリオレフイy ) (Tmo) :
TCDと同様の条件で測定。(7) Melting point (Boriolephiy) (Tmo):
Measured under the same conditions as TCD.
(8) 引張@撃強度(Ia) :テスター産業株
式会社Fil Tongile Impact Ta5
terにて測定。(8) Tensile @impact strength (Ia): Tester Sangyo Co., Ltd. Fil Tongile Impact Ta5
Measured at ter.
(9) 耐熱収縮性C3v) : )レイ型容器の
容積収都軍を230℃10分間の熱処理条件で611j
定。(9) Heat Shrinkage Resistance C3v): ) The capacity of the lay-type container was heat treated at 230°C for 10 minutes.
Fixed.
θI 離型性:成形体を金型(4)よシI@型せしめた
際の形状のくずれた状態にて評価。θI Mold release property: Evaluated in a state where the shape is collapsed when the molded product is pressed into the mold (4).
Oυ 賦型性:熱成形により潜られた成形体の金型トレ
ース性或いは形状欠陥を評価。Oυ Moldability: Evaluate the mold traceability or shape defects of the molded product that has been submerged by thermoforming.
QX5 ヒート/−脂性:容器の被に材シール部と蓋
材とを15IIJ巾でヒートシーラー“K上り熱接着し
、接着強度を引張試験機により測定。QX5 Heat/- Greasy: The material sealing part and the lid material were thermally bonded to the cover of the container with a width of 15IIJ using a heat sealer "K" and the adhesive strength was measured using a tensile tester.
米東洋テスター嘲り製T−45型ヒートシーラー
0 耐加熱滅菌性:ヒートシールしたサンプルを湿熱滅
菌処理袋@lf=’N (レトルト性)内で120℃に
て30分間処理した後、接着強度を引張試験機により測
定。T-45 type heat sealer 0 made by Toyo Tester Kagari (USA) Heat sterilization resistance: After processing the heat-sealed sample at 120°C for 30 minutes in a moist heat sterilization processing bag @lf='N (retortable), the adhesive strength was evaluated. Measured using a tensile tester.
硅 ヤマト科学■MSM−21型オートクレーブ
なお、ヒートシール性の評価は接着強度が1匂/ 15
+am以上の場合:○(良好)0.3〜1恥/15u
の場合:Δ(やや良好)0、3 K9/ 15 mm以
下の場合:×(不良)とした。Silk Yamato Scientific MSM-21 type autoclave The heat sealability evaluation was based on adhesive strength of 1 odor/15
+am or more: ○ (good) 0.3-1 shame/15u
In the case of: Δ (slightly good) 0, 3 In the case of K9/15 mm or less: × (poor).
またレトルト性は、ヒートシール性の評価と同様に実施
した。Further, retortability was evaluated in the same manner as the evaluation of heat sealability.
但し、容器の変形が大きいものも×(不良)とした。However, containers with large deformation were also rated as × (defective).
実施例1〜6及び比較例1〜5及び参考例I V 1.
08のホリエチレンテレ7タレート(以下PETと略記
する)を160℃で5時間熱風乾燥して得られた乾チッ
プ100部とタルク0.4部とをブレンド後、先端にシ
ート押出用ダイスを装置しである3 0 rta lス
クリュー径の押出機に供給した。押出機シリンター設定
温度240〜280℃の条件にて溶融混練し、押出シー
トを冷却ロールにて冷却して肉厚的0.5 Iuのポリ
エステルシートを得た。Examples 1 to 6, Comparative Examples 1 to 5, and Reference Example I V 1.
After blending 100 parts of dry chips obtained by drying No. 08 polyethylene tere-7 tallate (hereinafter abbreviated as PET) with hot air at 160°C for 5 hours and 0.4 part of talc, a die for sheet extrusion was attached to the tip. The mixture was fed into an extruder with a 30 rtal screw diameter. The mixture was melt-kneaded at an extruder cylinder temperature of 240 to 280°C, and the extruded sheet was cooled with a cooling roll to obtain a polyester sheet with a thickness of 0.5 Iu.
該ポリエステルシートは7278℃、融点(TmFJ)
250℃、 TCI 135℃、TcD190℃、ρ0
1.338f/i(結晶化度4%)、IVo、93であ
った。The polyester sheet has a melting point (TmFJ) of 7278°C.
250℃, TCI 135℃, TcD 190℃, ρ0
It was 1.338 f/i (crystallinity 4%) and IVo 93.
該シートを浅野研究所製FC−IAPA−W型圧空・真
空成形機によシ金型として′電熱ヒーターを挿入しであ
る彫込形状、たて135 mm 、 Wi 58U、深
さ181gの凹型トレイ型を、冷却用部材として内部に
冷却水を通水しであるたて140U、横65 ram
+厚さ40.の平板型を用い、表−1に示す条件にて真
空成形を行った。密度測定値及び成形性・成形体評価結
果を表−1に示す。The sheet was put into a FC-IAPA-W type compressed air/vacuum forming machine manufactured by Asano Research Institute as a mold into a concave tray with an electric heater inserted and an engraved shape, height 135 mm, Wi 58U, depth 181 g. The mold is made by running cooling water inside as a cooling member. Vertical 140U, horizontal 65 ram
+Thickness 40. Vacuum forming was performed using a flat plate mold under the conditions shown in Table 1. Table 1 shows the density measurement values and moldability/molded body evaluation results.
なお、冷却用部材は、シートを金型にでA、生成形開始
した直後に容器のM何シール部に接触せしめた。The cooling member was brought into contact with the sealing portion of the container immediately after the sheet was placed in the mold and forming was started.
第1図及び第2図にその概要を示す。The outline is shown in Fig. 1 and Fig. 2.
なお、蓋材には肉厚100μmのシートを3.3倍×1
3倍の倍率で2軸延伸した後、200℃で熱固定したP
ETフィルムの片面に酸成分としてイソフタル酸を40
モル%、グリコール成分としてジエチレングリコールを
12モルチ共重合せしめたI’ET(融点157℃)を
約15μmの厚さンこコートせしめたものを使用した。In addition, for the lid material, a sheet with a wall thickness of 100 μm was used 3.3 times
P that was biaxially stretched at a magnification of 3 times and then heat-set at 200°C.
40% of isophthalic acid as an acid component on one side of the ET film.
I'ET (melting point: 157° C.), which was copolymerized with 12 moles of diethylene glycol as a glycol component, was coated with a thickness of about 15 μm.
表−1より明らかな様に、金型u m:がPBTの結晶
化温度域より外れた比較列−4,5及び参考「11の場
合ではヒートシール性が良好であっても成形性或いは容
器の耐熱性が不良であり、また金型温度がPETの結晶
化温度域であっても比較例−1の如き従来の方法或いは
比較ff1l −2,3の如く冷却部材による冷却が不
十分の場合は、容器の側熱性はa好であるが、ヒートシ
ール性が不良となる。As is clear from Table 1, in the case of comparison rows 4 and 5 and reference 11, in which the mold u m: is outside the crystallization temperature range of PBT, even if the heat sealability is good, the moldability or container The heat resistance is poor, and even if the mold temperature is within the crystallization temperature range of PET, cooling by the conventional method as in Comparative Example-1 or cooling by the cooling member as in Comparative Example-2 and 3 is insufficient. In this case, the side heat resistance of the container is good, but the heat sealability is poor.
仁れに対し、実施例−1〜6の本発明では、耐7A +
%・ヒートシール性・レトルト性がいずれも良好であり
、実施例−1〜3及び6のものが特に優れる。In the present invention of Examples 1 to 6, resistance to 7A +
%, heat sealability, and retortability, and those of Examples 1 to 3 and 6 are particularly excellent.
実施例7.8及び比較例6
メルトインデツクス1.3の線状低密度ポリエチレンを
3重量部添加し、タルクを無添加としたほかは実施例1
と同様に押出機に供給し、肉厚約0.6uのポリエステ
ルシートを得た。Example 7.8 and Comparative Example 6 Example 1 except that 3 parts by weight of linear low density polyethylene with a melt index of 1.3 was added and no talc was added.
The mixture was fed to an extruder in the same manner as above to obtain a polyester sheet with a wall thickness of about 0.6 u.
該ポリエステルシートはTf 74℃、 TmE249
’C、Tm0101℃、 TCI 135℃、 Tco
182’C、,11101,327f /ad (結
晶化度5%)であった。The polyester sheet has a Tf of 74°C and a TmE of 249.
'C, Tm0101℃, TCI 135℃, Tco
182'C, ,11101,327f/ad (crystallinity 5%).
該シートを実施例1と同様に表−2に示す条件で真空成
形した。The sheet was vacuum formed in the same manner as in Example 1 under the conditions shown in Table 2.
密度測定値及び成形性、成形体評価結果を表−2に示す
。Table 2 shows the density measurement values, moldability, and molded body evaluation results.
本発明のものは耐熱性・ヒート7−ル性とも良好であっ
た。The material of the present invention had good heat resistance and heat resistance.
第1図は本発明における容器の成形状況を示す断面図で
あシ、第2図は成形後、容器を金型及び冷却用部材から
分離した状態を示す断面図である。
図面において、1はポリエステル容器、2は真空又り圧
空成形用金型、3は冷却用部材、4は容器の底部、5は
容器の側部、6は低結晶化状態である容器の蓋材との熱
接着部、7は金型の真空用又はぺ/ト用孔の1部、8祉
冷却用部材の圧空導入孔又はベント用孔の1部、9は冷
却用部材の容器との接着部をそれぞれ示す。FIG. 1 is a sectional view showing how the container is molded in the present invention, and FIG. 2 is a sectional view showing the container separated from the mold and the cooling member after molding. In the drawings, 1 is a polyester container, 2 is a vacuum or pressure molding mold, 3 is a cooling member, 4 is a bottom of the container, 5 is a side of the container, and 6 is a lid material for the container that is in a low crystallization state. 7 is a part of the vacuum or plastic hole of the mold, 8 is a part of the compressed air introduction hole or vent hole of the cooling member, 9 is the adhesion of the cooling member to the container. The parts are shown respectively.
Claims (3)
器であつて、ポリエチレンテレフタレートを主たる構成
成分とするポリエステル製シートを成形して得たもので
あり、前記熱接着部の結晶化度が20%未満であり、該
容器の底部及び(又は)側部の結晶化度が20%以上で
あることを特徴とするポリエステル容器。(1) A container equipped with a heat-bonded part for heat-bonding it to a lid material, which is obtained by molding a polyester sheet containing polyethylene terephthalate as a main component, and the heat-bonded part is crystallized. A polyester container, characterized in that the degree of crystallinity of the bottom and/or side portion of the container is 20% or more.
するポリエステル製シートを結晶化度が20%未満の状
態で加熱可塑化せしめ、次いで該ポリエステルの結晶化
温度範囲に保たれた金型により熱成形して容器を製造す
るに際し、該容器の蓋材との熱接着部を冷却用部材に接
触せしめて該熱接着部の結晶化を抑制することからなる
ポリエステル容器の製造法。(2) A polyester sheet containing polyethylene terephthalate as a main component is heat-plasticized with a degree of crystallinity of less than 20%, and then thermoformed into a container using a mold maintained within the crystallization temperature range of the polyester. 1. A method for producing a polyester container, which comprises bringing a thermally bonded portion of the container to a lid material into contact with a cooling member to suppress crystallization of the thermally bonded portion.
り20℃高温を上限とする温度範囲である特許請求の範
囲第2項記載のポリエステル容器の製造法。(3) The method for producing a polyester container according to claim 2, wherein the temperature of the cooling member is within a temperature range of 20° C. higher than the glass transition point of the polyester.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61072442A JPS62231720A (en) | 1986-04-01 | 1986-04-01 | Polyester vessel and its manufacture |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61072442A JPS62231720A (en) | 1986-04-01 | 1986-04-01 | Polyester vessel and its manufacture |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62231720A true JPS62231720A (en) | 1987-10-12 |
JPH0436534B2 JPH0436534B2 (en) | 1992-06-16 |
Family
ID=13489405
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61072442A Granted JPS62231720A (en) | 1986-04-01 | 1986-04-01 | Polyester vessel and its manufacture |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62231720A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09132272A (en) * | 1995-11-06 | 1997-05-20 | Toppan Printing Co Ltd | Easily openable container |
JP2001260215A (en) * | 2000-03-14 | 2001-09-25 | Toyobo Co Ltd | Producing method for vessel consisting of crystalline polyester sheet |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3678112B2 (en) * | 2000-05-12 | 2005-08-03 | 東洋製罐株式会社 | Heat resistant container |
-
1986
- 1986-04-01 JP JP61072442A patent/JPS62231720A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09132272A (en) * | 1995-11-06 | 1997-05-20 | Toppan Printing Co Ltd | Easily openable container |
JP2001260215A (en) * | 2000-03-14 | 2001-09-25 | Toyobo Co Ltd | Producing method for vessel consisting of crystalline polyester sheet |
Also Published As
Publication number | Publication date |
---|---|
JPH0436534B2 (en) | 1992-06-16 |
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