JPS5836408A - Manufacture of polyester molded item - Google Patents
Manufacture of polyester molded itemInfo
- Publication number
- JPS5836408A JPS5836408A JP13355681A JP13355681A JPS5836408A JP S5836408 A JPS5836408 A JP S5836408A JP 13355681 A JP13355681 A JP 13355681A JP 13355681 A JP13355681 A JP 13355681A JP S5836408 A JPS5836408 A JP S5836408A
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- layer
- polyester
- molded item
- polypropylene
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920000728 polyester Polymers 0.000 title claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 7
- 239000002131 composite material Substances 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims description 9
- 238000007666 vacuum forming Methods 0.000 claims description 5
- -1 polypropylene Polymers 0.000 abstract description 23
- 229920000139 polyethylene terephthalate Polymers 0.000 abstract description 11
- 239000005020 polyethylene terephthalate Substances 0.000 abstract description 11
- 239000004743 Polypropylene Substances 0.000 abstract description 10
- 229920001155 polypropylene Polymers 0.000 abstract description 10
- 238000000465 moulding Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 239000000470 constituent Substances 0.000 abstract 3
- LLLVZDVNHNWSDS-UHFFFAOYSA-N 4-methylidene-3,5-dioxabicyclo[5.2.2]undeca-1(9),7,10-triene-2,6-dione Chemical group C1(C2=CC=C(C(=O)OC(=C)O1)C=C2)=O LLLVZDVNHNWSDS-UHFFFAOYSA-N 0.000 abstract 1
- 230000035939 shock Effects 0.000 abstract 1
- 238000004806 packaging method and process Methods 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- NNBZCPXTIHJBJL-UHFFFAOYSA-N decalin Chemical compound C1CCCC2CCCCC21 NNBZCPXTIHJBJL-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- MMINFSMURORWKH-UHFFFAOYSA-N 3,6-dioxabicyclo[6.2.2]dodeca-1(10),8,11-triene-2,7-dione Chemical group O=C1OCCOC(=O)C2=CC=C1C=C2 MMINFSMURORWKH-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000012773 agricultural material Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229920006125 amorphous polymer Polymers 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 150000002085 enols Chemical class 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 238000007765 extrusion coating Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 229920000554 ionomer Polymers 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 239000002667 nucleating agent Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920005629 polypropylene homopolymer Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 229920005604 random copolymer Polymers 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- PXXNTAGJWPJAGM-UHFFFAOYSA-N vertaline Natural products C1C2C=3C=C(OC)C(OC)=CC=3OC(C=C3)=CC=C3CCC(=O)OC1CC1N2CCCC1 PXXNTAGJWPJAGM-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- B29C51/00—Shaping by thermoforming, i.e. shaping sheets or sheet like preforms after heating, e.g. shaping sheets in matched moulds or by deep-drawing; Apparatus therefor
- B29C51/14—Shaping by thermoforming, i.e. shaping sheets or sheet like preforms after heating, e.g. shaping sheets in matched moulds or by deep-drawing; Apparatus therefor using multilayered preforms or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/10—Polymers of propylene
- B29K2023/12—PP, i.e. polypropylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2067/00—Use of polyesters or derivatives thereof, as moulding material
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は高い衝撃強度と耐熱性を有するポリエステル製
成形品の製造方法に関するものであり、その目的とする
ところ蚤家4IKポリニスデル製深絞り成形品の耐衝撃
性及び耐熱性を改善する製造方法を提供することにある
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a polyester molded product having high impact strength and heat resistance, and its purpose is to improve the impact resistance and heat resistance of a deep-drawn molded product made of Flea 4IK polynisdel. The purpose of the present invention is to provide a manufacturing method that improves properties.
ポリエチレンテレフタレートのシート状物は従来二軸蔦
伸フィルムとして電気物品、印刷分野、農業資材及び包
装分野等に広(使用され【きた、極く景近ではポリエチ
レンテレフタレートを用いたトレー或いは深絞り成形品
であるカップ等が食品包装分野に使用され始めている。Sheets of polyethylene terephthalate have traditionally been used as biaxially stretched films in electrical goods, printing fields, agricultural materials, and packaging fields. Cups and the like are beginning to be used in the food packaging field.
ところでポリエチレンテレフタレートは結晶性高分子で
ありながらその結晶化速度はポリエチレン、ポリプロピ
レン或いはポリアミド等に比べ遅いため溶融状態から急
冷することにより非晶質のシートを得ることができる。Although polyethylene terephthalate is a crystalline polymer, its crystallization rate is slower than that of polyethylene, polypropylene, polyamide, etc., and therefore an amorphous sheet can be obtained by rapidly cooling it from a molten state.
この結果透明性の高いシートを得ることができる。As a result, a highly transparent sheet can be obtained.
またポリエチレンテレフタレートは結晶性高分子である
ため、蔦伸倍率が約2倍を超すと分子の配向効果及び結
晶化促進の効果により強靭さが蔦伸倍率と共に増大する
。この結果ポリ塩化ビニル、ポリスチレン等の非晶性高
分子に比べ深絞り成形した場合の成形品の肉厚を均一に
することができる。さらに非品性で透明なシートを鴬伸
して結晶化させた場合結晶化度が高くてもシートが白化
することはない。Furthermore, since polyethylene terephthalate is a crystalline polymer, when the stretch ratio exceeds about 2 times, the toughness increases with the stretch ratio due to the molecular orientation effect and the effect of promoting crystallization. As a result, compared to amorphous polymers such as polyvinyl chloride and polystyrene, the thickness of the molded product can be made more uniform when deep drawing is performed. Furthermore, when a non-quality transparent sheet is crystallized by stretching, the sheet does not turn white even if the degree of crystallinity is high.
これらの理由からポリエチレンテレフタレートの熱成形
品は透明性が高く2強靭なものとなる。For these reasons, thermoformed polyethylene terephthalate products are highly transparent and tough.
しかしながら上記ポリエチレンテレフタレート製深絞り
成形品はその側壁は殆んど一軸蔦伸された状態である。However, the side walls of the deep-drawn product made of polyethylene terephthalate are almost uniaxially elongated.
このため通常の包装用途に向ける場合には全く支障をき
たすことはないが苛酷な条件で使用する場合1例えば7
0℃近い温度で飲料物を充填し氷点下の温度で落下テス
トするような場合には側壁部に幾分縦割れが発生する欠
点がある。For this reason, there is no problem at all when using it for normal packaging purposes, but when using it under harsh conditions, for example 7
When a beverage is filled at a temperature close to 0° C. and a drop test is performed at a temperature below freezing, there is a drawback that some vertical cracks occur in the side wall portion.
本発明看はかかる欠点のない成形品を製造する方法につ
いて鋭意検討した結果ポリエステルシート層とポリエス
テルシート層の少なくとも二層からなる複合シートを特
定温度範囲にて成形品の最内層がポリエステルシート層
となるように深絞り成形することにより上記欠点のない
成形品とし得ることを見出し本発明に到達した。As a result of intensive studies on a method for manufacturing a molded product free from such defects, the present invention has developed a composite sheet consisting of at least two layers, a polyester sheet layer and a polyester sheet layer, in a specific temperature range so that the innermost layer of the molded product becomes a polyester sheet layer. The present invention was achieved by discovering that a molded product free from the above-mentioned drawbacks can be obtained by deep drawing.
即ち本発明の要旨とするところはポリエステルシート層
トポリプロピレンシート屡の少なくとも2層からなる複
合シートを160〜230℃の温[K加熱し、成形品の
最内層がポリエステルシート層となるように深絞り真空
成形することを峙黴とするポリエステル製成形品の製造
方法にある。That is, the gist of the present invention is to heat a composite sheet consisting of at least two layers, a polyester sheet layer and a polypropylene sheet, to a temperature of 160 to 230°C [K], and deep-ply it so that the innermost layer of the molded product becomes the polyester sheet layer. A method for manufacturing polyester molded products that uses drawing and vacuum forming to eliminate mold.
本発明を実施するに際して用いるポリニスデルとは繰り
返し単位数の80−以上がエチレンテレフタレート単位
よりなるポリエチレンテレフタレート又はエチレンテレ
フタレート共重合体、さらにはポリエチレンテレフタレ
ートが80重量−以上、他の熱可履性樹脂が20重量−
以下から構成される樹*S合物をさすものである。The polynisdel used in carrying out the present invention is polyethylene terephthalate or ethylene terephthalate copolymer in which the number of repeating units is 80 or more ethylene terephthalate units, furthermore, polynisdel is 80 or more by weight of polyethylene terephthalate, and other thermoplastic resins are 20 weight-
It refers to a tree*S compound consisting of the following:
前記ポリエステルには必要に応じ他の添加剤。Other additives may be added to the polyester as necessary.
例えばプ四ツキング防止剤、核形成剤等を含有せしめて
もよい。For example, it may contain an anti-quaking agent, a nucleating agent, and the like.
また本発−を実施するに際して用いるポリプロピレンと
はポリプロビレンホモボリマー、耐衝撃性の改良された
ランダムコポリマー或いはブロックコポリマーをさすも
のである。Further, the polypropylene used in carrying out the present invention refers to a polypropylene homopolymer, a random copolymer or a block copolymer with improved impact resistance.
本発明において用いる複合シートは上記ポリエステル及
びポリプロピレンの夫々のシート層の少なくとも二層か
ら構成されるものであり。The composite sheet used in the present invention is composed of at least two sheet layers of the above-mentioned polyester and polypropylene.
三層以上の場合には少な(とも最外層の一層がポリエス
テルシート層から構成されてい慝ことが必要である。上
記複合シートはいかなる方法によって製造してもよいが
、一般にはポリエステルシートにポリプロピレンを押出
しコーティングする方法がよい。ポリエステルシートと
ボリプwsヒレンシートとの接着性を向上するためにエ
チレン−酢酸ビニルエマルジョン接着剤。In the case of three or more layers, it is necessary that one of the outermost layers is composed of a polyester sheet layer.The above composite sheet may be manufactured by any method, but in general, polypropylene is added to a polyester sheet. Extrusion coating method is preferred. Ethylene-vinyl acetate emulsion adhesive to improve adhesion between polyester sheet and Volip WS Hiren sheet.
アイオノマー等を塗布してもよい。An ionomer or the like may be applied.
上記複合シートを深絞り成形するには従来の真空深絞り
成形技術の全べての方法を使用することができるが、プ
ラグで予備蔦伸し圧9を併用した真空成形法が好ましい
。深絞り真空成形する際に複合シートを160〜230
℃の温度に加熱し成形することが必要である。この範囲
の温度に加熱して深絞り成形するとポリエステルは弧伸
されても分子配向を殆んど起さない為得られる成形品の
引裂強度が強くなり前記したような縦割れ現象を抑える
ことができる。160℃未溝の温度で加熱して成形した
場合にはポリニスデルが分子配向し、その結果成形品側
壁の縦割れが生じやすくなる。また230℃を超える温
度下では安定した成形を行うことができなくなるので好
ましくない。All conventional vacuum deep drawing techniques can be used to deep draw the composite sheet, but a vacuum forming method using a pre-stretching pressure 9 with a plug is preferred. 160-230 when the composite sheet is deep drawn and vacuum formed
It is necessary to heat and shape the product to a temperature of °C. When polyester is heated to a temperature in this range and deep drawn, it hardly causes any molecular orientation even if it is arc-stretched, so the tear strength of the resulting molded product becomes strong and the vertical cracking phenomenon described above can be suppressed. can. When molded by heating at a temperature of 160° C. without grooves, polynisdel molecules become oriented, and as a result, vertical cracks tend to occur in the side walls of the molded product. Moreover, it is not preferable to perform stable molding at a temperature exceeding 230°C.
本発明において深絞り真空成形するに際しては得られる
成形品の最内層が前記複合シートを構成するポリエステ
ルシート層となるように行うことが必要である。これK
より例えば種々の飲料物を充填しても衛生的に優れてい
るため問題を生じない。In the present invention, deep drawing and vacuum forming must be carried out so that the innermost layer of the resulting molded product becomes the polyester sheet layer constituting the composite sheet. This is K
For example, even if the container is filled with various beverages, no problem arises because it is hygienic.
本発明は低温落下時に縦割れの生じない、また高温での
形態安定性に優れた高耐衝撃強度と高耐熱性を有する深
絞り成形品を容易に製造することができる特徴な有する
。The present invention has the characteristic that it is possible to easily produce a deep-drawn product that does not cause vertical cracking when dropped at low temperatures, has excellent shape stability at high temperatures, and has high impact strength and high heat resistance.
以下実施flKより本発明を具体的に説明する。The present invention will be specifically explained below based on the implementation example.
なおポリエチレンテレフタレート及びポリプロピレンの
極限粘度は次の方法で測定したものである。Note that the intrinsic viscosity of polyethylene terephthalate and polypropylene was measured by the following method.
ポリエチレンテレフタレートの極限粘度=7エノール/
Tトラクロロエタン(50150重量比)混合溶媒にポ
リマーを溶かし25℃で測定した。Intrinsic viscosity of polyethylene terephthalate = 7 enol/
The polymer was dissolved in a mixed solvent of T-trachloroethane (50,150 weight ratio) and measured at 25°C.
ポリプロピレンの極限粘度: デカリンを溶媒として135℃で測定した。Intrinsic viscosity of polypropylene: Measurement was carried out at 135°C using decalin as a solvent.
実施例1
極限粘度0.73のポリエチレンテレフタレートからな
4厚さ0.2 mIlのシート二層の間に極限粘度1.
5ノポリプロピレンを厚さ0. I mになるようVC
5’ネートした三層からなる複合シートを高速インライ
ン連続真空成形機にかけ、自径70m、絞り比1.35
の深絞りカップ成形品を36ケ取りで成形した。成形前
のシート温[は175℃であった。Example 1 A sheet of polyethylene terephthalate having an intrinsic viscosity of 0.73 and an intrinsic viscosity of 1.2 ml was placed between two layers of 4 0.2 ml thick sheets.
5-no polypropylene with a thickness of 0. VC to become I m
A composite sheet consisting of three 5'-layered layers was applied to a high-speed inline continuous vacuum forming machine with an own diameter of 70 m and a drawing ratio of 1.35.
A deep-drawn cup molded product was molded using 36 cavities. The sheet temperature before molding was 175°C.
得られた深絞りカップ成形品を紙製カップに内挿し一体
化した後、67℃の熱湯を全容積の9割だけ充填し直ち
に感熱接着剤を塗布したアルミ箔でシールし、3℃に冷
却した。冷却後150cILの高さから100ケ落下さ
せたところ破損は全(発生しなかった。After inserting and integrating the obtained deep-drawn cup molded product into a paper cup, 90% of the total volume was filled with 67°C hot water, immediately sealed with aluminum foil coated with heat-sensitive adhesive, and cooled to 3°C. did. After cooling, 100 pieces were dropped from a height of 150 cIL, and no damage occurred.
比較例1
1[1[i度0.73のポリエチレンプレ7タレートよ
りなる厚さ0.5 mのシートを実施例1と同じ真空成
形機で深絞り成形し、実施例1と同じ方法で落下テスト
を行ったところ破損率は85−に達した。Comparative Example 1 A 0.5 m thick sheet made of polyethylene pre-7 tallate with a degree of When tested, the failure rate reached 85-.
Claims (1)
とも二層からなる複合シートを160〜230℃の温度
に加熱し、成形品の最内層がポリニスデルシート層とな
るように深絞り真空成形することを特徴とするポリエス
テル製成形品のll造方法。A composite sheet consisting of at least two layers, a polyester sheet layer and a polyester sheet layer, is heated to a temperature of 160 to 230°C, and deep drawing vacuum forming is performed so that the innermost layer of the molded product becomes a polynisdel sheet layer. A method for manufacturing polyester molded products.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13355681A JPS5836408A (en) | 1981-08-26 | 1981-08-26 | Manufacture of polyester molded item |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13355681A JPS5836408A (en) | 1981-08-26 | 1981-08-26 | Manufacture of polyester molded item |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5836408A true JPS5836408A (en) | 1983-03-03 |
Family
ID=15107564
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13355681A Pending JPS5836408A (en) | 1981-08-26 | 1981-08-26 | Manufacture of polyester molded item |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5836408A (en) |
-
1981
- 1981-08-26 JP JP13355681A patent/JPS5836408A/en active Pending
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