TW210976B - Multi-layer refillable container having higher wash temperature and redvced product flavor carryover, preform and method of forming same - Google Patents
Multi-layer refillable container having higher wash temperature and redvced product flavor carryover, preform and method of forming same Download PDFInfo
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- TW210976B TW210976B TW81106831A TW81106831A TW210976B TW 210976 B TW210976 B TW 210976B TW 81106831 A TW81106831 A TW 81106831A TW 81106831 A TW81106831 A TW 81106831A TW 210976 B TW210976 B TW 210976B
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- Prior art keywords
- container
- layer
- prototype
- copolymer
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- 238000000034 method Methods 0.000 title claims description 23
- 239000000796 flavoring agent Substances 0.000 title abstract 2
- 235000019634 flavors Nutrition 0.000 title abstract 2
- 239000010410 layer Substances 0.000 claims abstract description 75
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- 239000000463 material Substances 0.000 claims abstract description 37
- 239000012792 core layer Substances 0.000 claims abstract description 33
- 238000002425 crystallisation Methods 0.000 claims abstract description 21
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- -1 polyethylene terephthalate Polymers 0.000 claims description 17
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 12
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 12
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
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- 239000013078 crystal Substances 0.000 claims description 2
- 238000001746 injection moulding Methods 0.000 claims 3
- 239000002344 surface layer Substances 0.000 claims 2
- 125000001140 1,4-phenylene group Chemical group [H]C1=C([H])C([*:2])=C([H])C([H])=C1[*:1] 0.000 claims 1
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- 239000005977 Ethylene Substances 0.000 claims 1
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- 238000002347 injection Methods 0.000 abstract description 19
- 239000007924 injection Substances 0.000 abstract description 19
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- 229920003023 plastic Polymers 0.000 abstract description 6
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- 238000007664 blowing Methods 0.000 description 7
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- YIMQCDZDWXUDCA-UHFFFAOYSA-N [4-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1CCC(CO)CC1 YIMQCDZDWXUDCA-UHFFFAOYSA-N 0.000 description 5
- 239000000178 monomer Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 4
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
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- 238000003860 storage Methods 0.000 description 3
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- 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 2
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- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
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- 235000015203 fruit juice Nutrition 0.000 description 2
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- 229920001519 homopolymer Polymers 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
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- 238000005259 measurement Methods 0.000 description 2
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- 239000008267 milk Substances 0.000 description 2
- 235000013336 milk Nutrition 0.000 description 2
- 210000004080 milk Anatomy 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- BDJRBEYXGGNYIS-UHFFFAOYSA-N nonanedioic acid Chemical compound OC(=O)CCCCCCCC(O)=O BDJRBEYXGGNYIS-UHFFFAOYSA-N 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 229920001225 polyester resin Polymers 0.000 description 2
- 239000004645 polyester resin Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000002356 single layer Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- ARCGXLSVLAOJQL-UHFFFAOYSA-N trimellitic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C(C(O)=O)=C1 ARCGXLSVLAOJQL-UHFFFAOYSA-N 0.000 description 2
- 230000000007 visual effect Effects 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-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
- SENMPMXZMGNQAG-UHFFFAOYSA-N 3,4-dihydro-2,5-benzodioxocine-1,6-dione Chemical compound O=C1OCCOC(=O)C2=CC=CC=C12 SENMPMXZMGNQAG-UHFFFAOYSA-N 0.000 description 1
- 241000283690 Bos taurus Species 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- BDAGIHXWWSANSR-UHFFFAOYSA-M Formate Chemical compound [O-]C=O BDAGIHXWWSANSR-UHFFFAOYSA-M 0.000 description 1
- 206010067482 No adverse event Diseases 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- 229920001283 Polyalkylene terephthalate Polymers 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 206010041349 Somnolence Diseases 0.000 description 1
- 241000270666 Testudines Species 0.000 description 1
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 1
- ORLQHILJRHBSAY-UHFFFAOYSA-N [1-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1(CO)CCCCC1 ORLQHILJRHBSAY-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 229920005605 branched copolymer Polymers 0.000 description 1
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 235000019993 champagne Nutrition 0.000 description 1
- 229920006026 co-polymeric resin Polymers 0.000 description 1
- QYQADNCHXSEGJT-UHFFFAOYSA-N cyclohexane-1,1-dicarboxylate;hydron Chemical compound OC(=O)C1(C(O)=O)CCCCC1 QYQADNCHXSEGJT-UHFFFAOYSA-N 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
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- 125000001142 dicarboxylic acid group Chemical group 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
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- GTZOYNFRVVHLDZ-UHFFFAOYSA-N dodecane-1,1-diol Chemical compound CCCCCCCCCCCC(O)O GTZOYNFRVVHLDZ-UHFFFAOYSA-N 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- ACCCMOQWYVYDOT-UHFFFAOYSA-N hexane-1,1-diol Chemical compound CCCCCC(O)O ACCCMOQWYVYDOT-UHFFFAOYSA-N 0.000 description 1
- 125000004051 hexyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 150000007857 hydrazones Chemical class 0.000 description 1
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- 239000004611 light stabiliser Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
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- 239000000314 lubricant Substances 0.000 description 1
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- 238000012986 modification 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
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-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
- 239000000049 pigment Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920001748 polybutylene Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 235000021395 porridge Nutrition 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
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- 230000002787 reinforcement Effects 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
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Landscapes
- Containers Having Bodies Formed In One Piece (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
經濟部屮央櫺準局只工消«·合作社印Μ 4UOQ7〇_ 五、發明説明(l) 本發明係關於 重塡性塑膠容器, 交流。 可回收且可重 場,自從大陸PET 大成長。此等回收 歐洲和中、南美洲 回收性和重塡 的掩埋和再製問題 器可以進入法律禁 獨佔的市場。目標在 可耐無數次的重塡 一般而言,重 是在20次以上循環 視爲經濟可行。迴 汚染物檢查,產品 零售據點,·和⑸由 回到裝瓶廠。其循 回收性/重塡 商業上可行性。包 1. 尚度清晰 查; 2. 整個容器 3. 對鹼洗引 5月 10日修正| 容器新穎而有用的改良,尤指一種多層 可耐較高鹸洗溫度,並減少產品的氣味 塡的PET碳酸氣軟性飮料(CSD)瓶的市 科技公司於1987年引進後,全球享有重 性/重塡性瓶已商業化,橫掃大部份的 ,如今已移師遠東市場。 性瓶可以減少現有廢棄塑膠飮料瓶相關 。此外,重塡瓶容許安全輕便的塑膠容 止使用非回收性包裝而且以前是由玻璃瓶 於生產重塡瓶,具有必要的物理特性, 循環,而且可經濟生產。 塡性塑膠瓶必須在至少1〇次以上,最好 或迴路,仍維持其功能和美感特點,方 路包括:⑴空瓶用熱鹼液洗淨,接着⑵ 充塡/加蓋,⑶倉儲,⑷分配至批發和 消費者購買、使用,和空瓶儲存,最後 環如第1圖所示% 性容器必須呈現若干關鍵標準,以達成 含: 性(透明性),得以在生產綫上目視檢 使用壽命上的尺寸安定性;和 起應力龜裂和破漏的抵抗性。 先 Μ 背 而 之 注 項 Λ 本·" 装 η 線 本紙張尺度边用中a Η家樣準(CHS)T4执怙(210x297公;》:) 81. 7. 20.000張(11> 經濟部+央榀準而员工消伢合作社印製 _ 五、發明説明(2) 已知商業化 苯二甲酸乙二酯 1,4-環己烷二甲 此瓶用之雛型壁 型的2至2.5倍 η 6 先 閲 讀 背 而 之 注 意 項 再 窍 本A £ 裝 線 此較大雛 (即 0.5 物含量可 。不宜有 器所需的 已知 性超過20 ,以提闻 產品氣味 產品(例 環中,滲 產品的味 高洗溫, 因此 壽命至少 減重塡旅 明下述達 依照 度水準, 型厚度 — 0.7 在射出 過度雛 商業化 商業化 次重塡 洗溫能 交流。 如麥根 透入第 道。爲 爲某些 ,需提 5次重 程間的 成0 本發明 同時維 容器,是由單層聚對 5 %共聚單體,諸如 二甲酸(ΙΡΑ),吹製 原在5 —7««之譜,或爲單次消耗瓶之雛 回收性/重塡性CSD (PET)形成,含3 -醇(CHDM)或異對苯 。基於所需PET平面 提供濫用抵抗性所需 »〇» ),以求瓶之長期 成型法中防止雛型形· 型渾濁,因爲有碍回 生產綫上目視檢查過 CSD容器在鹸洗溫度 旅程。雖然有成,但 力達65 °C,最好是70 後者之所以發生,是 啤酒)移到瓶側壁, 二種產品內(例如水 提高有效殺菌和/或 食品,例如果汁和牛 高回收瓶的容許鹼洗 塡旅程,最好超過10 產品氣味交流。上述 延伸比爲6 — 10:1 , 壁厚度 高共聚 即渾濁 飮料容 較大的平均瓶 尺寸安定性。 成目視結晶, 收性/重塡性 程。 60eC,證明現 商業上需要改 °C或以上,同 因氣味成份從 隨即在以後的 水),即影响 減少鹸洗時間 奶所需。 溫度在60 °C以 或20次重塡旅 和其他目的可 場可行 良容器 時減少 第一種 充塡循 第二種 ,需提 上,使 程,並 由本發 ,提供一種多層容器,增進表面側壁結晶 持高水準的透明性(清晰性),因而特別 2 本紙ft尺度遑用中a S家楳毕(CNS) T4規彷(210x297公4) 81· 7. 20.000张(II) Λ 6 Π 6 21097ο 五、發明説明(3) 適用於回收性/重塡性飮料瓶。容器在尺寸上 使用壽命至少5次重塡循環,更好是至少10或 環,且暴露於洗溫60°C和以上,最好是至少約 Ό和以上,可抵抗鹸洗引起的應力龜裂和洩漏 此係由提供多層側壁的雛型達成,包含第 共聚物聚酯,另一層爲第二聚酯,共聚物較第 。最好是由高共聚物聚酯形成芯層,在低共聚 層和外層之間。高共聚物芯層防止內部芯層的 濁),在射出過程中冷却更慢,以保存整體容 和檢驗性。外表(內和外)層在射出製程中冷 不易結晶。係由較高延伸率或應變引發結晶的 共聚物聚酯製成,因此提供增進對鹸引起應力 抵抗性,並減少吹製容器內的氣味交流。 芯層典型上包括側壁厚度之約50 — 80%, 爲佳。內層和外層的結晶度百分比,在約20 — 而芯層約〖4 ~ 20 %。 可安定跨越 20次重塡循 65 °C或約70 〇 一層爲第一 一聚酯爲少 物聚酯的內 結晶化(渾 器的清哳性 却較快,較 均聚物或低 龜裂的表面 以 60 — 70 % 28 %範圍, rh 先 KI ίίϊ 背 而 之— 注 孙 % 木 裝 訂 線 經濟部屮央標準局=5工消仰合作社印製 在較佳具體例中,使用計量的依序共射出法,生產二 種材料三層PET雛型,第一次射出均聚物或低共聚物,即 總重量〇 — 2 %的共聚物含量,以形成內層和外層,接着 第二次射出高共聚物,即總重量4 一 6%的共聚物含量, 形成芯層。此可達成容器側壁內約22 — 26 %的應變引發表 面結晶性水準,得典型雛型平面延伸比爲8 _10:1,結晶 度百分比遠較高共聚物芯層爲低。總之,與單層已知回收 性/重塡性CSD飮料瓶相較,此容器可在較髙溫度(65 ΐ 〜3〜 本紙法尺Λ边用中a Η家標』MCNS)T4規枋(210X297公;it) 81. 7. 20.000^(1!) 21097ο 五、發明説明(4) 和以上)洗淨,顯示減少氣味交流(改進20 %或以上), 容器性能無重大損失。 提高溫度時,對渾濁和應力龜裂抵抗性的改進,使本 發明容器特別適合做熱充塡容器° 還可利用熱定型技術,進一步增進表面結晶性水準至 30 %或以上。 本發明上述和其他特點,由如下詳述和附圖所示具韹 例,即可更爲明白。 第1圖爲回收性/重塡性容器必然經過的典型循環或 迴路之示意圖; 第2圖本發明1 . 5公升PET碳酸氣飮料瓶部份剖開之 示意立面圖,沿瓶的各種位置,表示高共聚物芯層與低共 聚物內層和外層相較之不同結晶度水準; 第3圖爲沿第2圖3 — 3綫之部份放大圖,詳示高共 聚物PET的中心芯層,以及低共聚物PET的內層和外層; 第4圖爲通過射出模腔的示意斷面圖,表示聚酯樹脂 材料引入模腔形成本發明雛型之方式; 經濟部屮央標準局貝工消"合作社印3i (請先間讀背而之注意事項外艰寫本頁) 第5圖爲部份放大示意圖,表示第一低共聚物材料量 射入模腔底部之方式,遇較冷模壁表面即冷却,以形成雛 型的內層和外層; 第6圖爲部份放大示意圖,表示第二高共聚物材料量 射入模腔底部,形成芯層之方式,造成第一和第二材料的 隧式流動,形成雛型; 第7圖爲製造本發明容器所用多層雛型之放大斷面圖;The Ministry of Economic Affairs, the Central Bureau of the Ministry of Economic Affairs only works to eliminate «· Cooperative Society Print Μ 4UOQ7〇_ V. Description of the invention (l) The present invention is about the exchange of heavy plastic containers. Recyclable and reusable, since the growth of mainland PET. These recycling and recycling and reprocessing devices in Europe, Central and South America can enter markets that are legally prohibited and exclusive. The goal is to endure countless times. Generally speaking, it is considered economically feasible to repeat more than 20 cycles. Return to the pollutant inspection, product retail base, and ⑸ from back to the bottling plant. Its recycling / heavy commercial viability. Package 1. The degree of clarity is clearly checked; 2. The entire container 3. Amendments to the alkaline washing on May 10 | The container is a novel and useful improvement, especially a multilayer that can withstand higher washing temperatures and reduce the smell of the product. After the introduction of the PET Carbonate Soft Cone (CSD) bottle by the city technology company in 1987, the world's heavy / heavy bottle has been commercialized, sweeping most of it, and has now moved to the Far East market. Sex bottles can reduce the existing waste plastic bottle related. In addition, heavy-duty bottles allow safe and lightweight plastics to use non-recyclable packaging. Previously, glass bottles were used to produce heavy-duty bottles, which have the necessary physical characteristics, recycling, and can be produced economically. The plastic bottle must be at least 10 times or better, or the circuit should still maintain its function and aesthetic characteristics. The square path includes: ⑴ the empty bottle is washed with hot alkaline solution, and then ⑵ filling / capping, ⑶ storage, ⑷Distribution to wholesale and consumer purchase, use, and storage of empty bottles, the final ring as shown in Figure 1% sex containers must present a number of key standards in order to achieve content: transparency (transparency), which can be used visually on the production line Dimensional stability in life; and resistance to stress cracking and leaking. The first note item of the back Λ Ben · " installed η line book paper standard side use a Η family sample standard (CHS) T4 execution (210x297 ;; :) 81. 7. 20.000 sheets (11> Ministry of Economic Affairs + Printed by the central government and printed by the employee ’s cooperative _ V. Description of the invention (2) Known commercial ethylene phthalate 1,4-cyclohexane dimethyl The prototype wall type used in this bottle is 2 to 2.5 Times η 6 Read the precautions first and then know this A £ Install the larger chick (ie 0.5 substance content is acceptable. It is not advisable to have a known value of more than 20 in order to smell the product smell product (for example, in the ring, The taste of the infiltrated product is high in washing temperature, so the life expectancy is at least weight-reducing. The following is up to the standard level, type thickness-0.7. In the case of excessive injection, commercialization, commercialization, and secondary washing temperature can communicate. For some, it is necessary to mention the formation of 0 between 5 times of the weight range. The simultaneous dimension container of the present invention is composed of a single layer of 5% comonomer, such as dicarboxylic acid (ΙΡΑ), blown in 5-7 «« The spectrum may be formed from the recyclable / heavy CSD (PET) of a single consumption bottle, containing 3-alcohol (CHDM) or isoparaben. The required PET surface provides the resistance required for abuse »〇»), in order to prevent the prototyping and turbidity in the long-term molding method of the bottle, because it hinders the visual inspection of the CSD container during the washing temperature journey back to the production line. Into the side wall of the bottle, within two products (such as water to increase effective sterilization and / or food, such as fruit juices and cattle high recovery bottles) On the journey of washing, it is better to exchange the odor of the product over 10. The above extension ratio is 6-10: 1, high wall thickness, copolymerization, that is, turbidity. The volume of the bottle is larger. The stability of the average bottle size is visual. Crystallization, yield / heavy process .60eC, which proves that it is necessary to change ° C or above in the commercial market, and the same odor components will be used in the subsequent water), that is, it will reduce the time required to wash the milk. The temperature is 60 ° C or 20 times. The purpose is to reduce the first type of filling when the container is feasible and follow the second type. It needs to be mentioned, and the process, and by the present invention, provides a multi-layered container to improve the crystallinity of the surface side wall to maintain a high level of transparency (clear ), So special 2 paper ft scales are used in a S home furniture (CNS) T4 standard (210x297 male 4) 81 · 7. 20.000 sheets (II) Λ 6 Π 6 21097ο V. Description of the invention (3) applies to Recyclable / heavy urn bottle. The service life of the container is at least 5 heavy gang cycles in size, preferably at least 10 or rings, and exposed to a wash temperature of 60 ° C and above, preferably at least about Ό and above, Resistant to stress cracks and leaks caused by flushing. This is achieved by providing a prototype with multiple layers of side walls, including the first copolymer polyester, and the other layer is the second polyester, the copolymer is the first. Preferably, the core layer is formed from a high copolymer polyester, between the low copolymer layer and the outer layer. The high copolymer core prevents turbidity of the inner core) and cools more slowly during the injection process to preserve the overall capacity and testability. The outer (inner and outer) layers are not easy to crystallize during the injection process. It is made of a copolymer polyester with higher elongation or strain-induced crystallization, thus providing improved resistance to emu-induced stress and reduced odor exchange within the blown container. The core layer typically includes about 50-80% of the thickness of the side walls, which is preferably. The crystallinity percentage of the inner layer and the outer layer is about 20 — while the core layer is about 4-20%. It can be stabilized across 20 repetition cycles of 65 ° C or about 70. One layer is the first polyester and the inner crystallization of the less polyester (the clearness of the turbidity is faster, which is more homopolymer or lower turtle). The cracked surface is in the range of 60-70% 28%, rh first KI ίίϊ back to the opposite-Note Sun% wood binding line Ministry of Economic Affairs, Central Bureau of Standards = 5 Gongxiaoyang cooperatives printed in the preferred specific example, using the metered Sequential co-injection method to produce two-material three-layer PET prototype, first injection of homopolymer or low copolymer, that is, the total weight of copolymer content of 0-2%, to form the inner layer and the outer layer, followed by the second Secondary injection of high copolymer, that is, copolymer content of 4 to 6% of the total weight, forms the core layer. This can achieve a strain-induced surface crystallinity level of about 22-26% in the side wall of the container, resulting in a typical prototype plane extension ratio of 8 _10: 1, the crystallinity percentage is much higher and the core layer of the copolymer is lower. In short, compared with the single-layer known recyclable / heavy CSD bottle, this container can be used at a relatively high temperature (65 l ~ 3 ~ this paper Law ruler Λ side use middle a Η home standard 』MCNS) T4 gauge (210X297 public; it) 81. 7. 20.000 ^ (1!) 21097ο V. Description of the invention (4) and above) Washing, showing reduced odor exchange (improved by 20% or more), without significant loss of container performance. The improvement of the resistance to turbidity and stress cracking when the temperature is increased makes the container of the present invention particularly suitable as a hot-filled container. The heat setting technology can also be used to further increase the surface crystallinity level to 30% or more. The above and other features of the present invention will be more apparent from the following detailed description and examples shown in the accompanying drawings. Figure 1 is a schematic diagram of a typical cycle or circuit that must be traversed by a recyclable / heavy container; Figure 2 is a schematic elevation view of a 1.5-liter PET carbon dioxide gas bottle partly broken away in the present invention, along various positions of the bottle , Indicating that the high copolymer core layer has different crystallinity levels compared to the inner and outer layers of the low copolymer; Figure 3 is an enlarged view of the part along the line 3-3 of Figure 2, detailing the center core of the high copolymer PET Layer, and the inner and outer layers of the low copolymer PET; Figure 4 is a schematic cross-sectional view through the injection of the cavity, showing the way the polyester resin material is introduced into the cavity to form the prototype of the present invention;工 消 " Cooperative printed 3i (please read back and forth and write this page) Figure 5 is a partially enlarged schematic diagram showing the way the first low copolymer material is injected into the bottom of the mold cavity. The surface of the cold mold wall is cooled to form the inner and outer layers of the prototype; Figure 6 is a partially enlarged schematic diagram showing that the second high copolymer material is injected into the bottom of the mold cavity to form the core layer, resulting in the first and The tunnel flow of the second material forms a prototype; Figure 7 shows the system The container of the present invention is an enlarged sectional view of a multilayer with the prototype;
A 本紙张尺度边用中a Η家炫毕(CNS) TM«m(21〇x29/公;«:) 81. 7. 20,000张(II) 經濟部中央楛準局员工消«·合作社印32.A This paper is used in the margin of the standard a Η 家 炫 毕 (CNS) TM «m (21〇x29 / 公;« :) 81. 7. 20,000 sheets (II) Employee consumption of the Central Bureau of Economic Development of the Ministry of Economic Affairs «· Cooperative cooperative printing 32 .
2109^ AG ______η 6______ 五、發明説明(5 ). 第8圖爲部份放大圖,表示第7圖雛型所製成容器基 部斷面圖; 第9圖爲雛型變通具體例之部份斷面圖,在雛型的形 成基部斷面具有第三射出材料,以代替芯材,可爲類似內 層和外層之低共聚物材料; 第10圖爲部份放大圖,表示第9圖雛型製容器基部之 斷面圖。 " 茲參見附圖,尤指第1圖,回收性/重塡性容器必須 耐受無數重塡循環,還能維持其美感和功能性特點。模擬 該循環的試驗程序如下。各容器經典型商業用鹸洗溶液, 是由3.5 %重量氫氧化鈉和自來水配製而成。洗液維持在 較高溫度,典型上約60 °C,按照本發明以至少約65。(:更佳 ,而以至少約7(TC尤佳。瓶脫蓋在洗液內浸15分鐘,模擬 商業化洗瓶系統之時間/溫度條件。自洗液取出後,瓶用 自來水冲洗,再於4·0±0.2大氣壓充塡碳酸氣水液(以 模擬碳酸氣軟性飮料的壓力),加蓋,置於50 %相對濕度 的38 °C對流烘箱內歷24小時。選擇此提升的烘箱溫度,旨 在模擬在較低周圍溫度時的較長商業上儲存期間。自烘箱取出 後,容器放空,再經同樣重塡循環,直至損壞。 損壞意指任何龜裂傳過瓶壁,造成洩漏和壓力損失。 容量收縮是將容器內部容量(基於室溫所能保存的液體容 量)在每次重塡循環前後加以比較而測定。本發明容器在 最好是65 °C或以上的洗溫,能耐至少5次,最好至少10或 20次此種重塡循環,而不損壞,容量變化不超過約1.5 % 5〜 本紙張尺度边用中a S家楳毕(CNS) TM規怙(210X297公龙) 81. 7. 20,000ik(||) (請先KJiftlrlru之注意事頊¾本頁) 裝· 210976 A 6 Π 6 五、發明説明(6 ) 。由氣體層析質譜測量,測得容器較已知商業化CSD瓶減 少產品氣味交流至少20 %。 第2圖表示按照本發明製 性PET碳酸氣飮料瓶。瓶1〇是 心本體,具有開口上端,頸部 (圖上未示),以及密封下底 直立側壁13,包含上斜肩部14 直立軸綫或中心綫CL限定) 有中央流道部20,內凹拱或凹 22,瓶靠此置放,以及徑向漸 渡至側壁16。瓶10之多層側壁 比例尺小之故。 第3圖表示胴部16側壁斷 以及低共聚物內層32和外層34 升容器高約13.2吋(335簡) t 92咖)。芯層30厚約0 . 0 15 — 厚各約0.003 — 0.006吋,根 成的1 .5公升回 一體吹氣成型的 12加工成陽螺紋 18。頸部和底部 ,和圓筒形胴部 。整體底部是香 部22,最低連續 增之外底部26, 並非具體如第2 收性/重塡 双軸導向空 以容納旋蓋 間爲實質上 16 (由瓶& 檳酒型底, 環部或凸邊 以供順利過 圖所示,因 vt 先 閲 背 而 注 意 事- 項 % 本 π 經濟部+央標準局工消伢合作社印5i ,平面延伸比約10: 1。平面延 度對平均瓶側壁厚度之比。容 重塡飮料瓶,較佳平面延伸比 佳。環圈延伸以3 _ 3.6:1爲 面,具有高共聚物芯層30, 。在特定具體例中,1.5公 ,(最寬)直徑約3.6吋( 0.024吋,內層32和外層34 據雛型的側壁厚約〇 . 230吋 伸比是根據平均雛型側壁厚 量約0.5 ~ 2.0公升的聚酯 約 7 — II: 1 ,以 8 — 10:1 爲 佳,軸錢延伸爲2 — 3:1。 此擧提供容器側壁有所需濫用抵抗性,而雛型側壁有所需 目視透明性。側壁厚度和選定延伸比,視特點瓶的尺寸, 內壓(例如,啤酒爲2.0大氣壓,軟性飮料爲4大氣壓) 〜6 ^, 木紙张尺度边用中a Η家標半(CHS)TM规彷(210x297公;it)2109 ^ AG ______ η 6______ V. Description of the invention (5). Figure 8 is a partially enlarged view showing the cross-sectional view of the base of the container made from the prototype of Figure 7; Figure 9 is a partial fracture of the specific example of the modification of the prototype The top view, with a third injection material at the base section of the prototype, instead of the core material, can be a low copolymer material similar to the inner layer and the outer layer; Figure 10 is a partially enlarged view showing the prototype of Figure 9 A sectional view of the base of the container. " Referring now to the drawings, especially Figure 1, the recyclable / heavy container must withstand countless cycles, and still maintain its aesthetic and functional characteristics. The test procedure to simulate this cycle is as follows. The classic commercial emu washing solution in each container is prepared from 3.5% by weight sodium hydroxide and tap water. The lotion is maintained at a relatively high temperature, typically about 60 ° C, and at least about 65 according to the present invention. (: Better, and at least about 7 (TC is particularly preferred. Immerse the bottle in the wash solution for 15 minutes to simulate the time / temperature conditions of a commercial bottle wash system. After the wash solution is taken out, rinse the bottle with tap water and then Filled with carbonated water at 4 · 0 ± 0.2 atmospheric pressure (to simulate the pressure of carbonic acid soft feed), covered and placed in a convection oven at 38 ° C with 50% relative humidity for 24 hours. Select this elevated oven temperature , Designed to simulate a longer period of commercial storage at lower ambient temperatures. After being removed from the oven, the container is emptied and then circulated again through the same weight until it is damaged. Damage means that any cracks pass through the bottle wall, causing leakage and Pressure loss. Volume shrinkage is measured by comparing the internal volume of the container (based on the liquid volume that can be stored at room temperature) before and after each heavy cycle. The container of the present invention is resistant to washing at a temperature of 65 ° C or above At least 5 times, preferably at least 10 or 20 times such heavy cycle, without damage, the capacity change does not exceed about 1.5% 5 ~ This paper is used in the edge of a S Jia Yu Bi (CNS) TM regulations (210X297 Dragon) 81. 7. 20,000ik (||) (Please KJiftlrlr first Note for u ¾ this page) Pack · 210976 A 6 Π 6 V. Description of the invention (6). The gas chromatography mass spectrometry measured the container to reduce the product odor exchange by at least 20% compared to the known commercial CSD bottles. Fig. 2 shows a PET carbonated gas bottle made according to the present invention. The bottle 10 is a core body with an open upper end, a neck (not shown in the figure), and a sealed bottom vertical wall 13 including an upper oblique shoulder 14 Line or center line CL is defined) There is a central flow channel portion 20, an inner concave arch or recess 22, the bottle is placed against this, and gradually radiates to the side wall 16. The multilayered side wall of the bottle 10 has a small scale. Figure 3 shows The side wall of the carcass 16 is broken and the inner layer 32 and the outer layer 34 of the low copolymer are about 13.2 inches (335 liters t 92 coffee tall). The thickness of the core layer 30 is about 0.015 — each thickness is about 0.003 — 0.006 inches, and the root is made of 1.5 liters. The integral blow-molded 12 is processed into a male thread 18. Neck and bottom, and cylindrical carcass. The overall bottom is the incense part 22, the lowest continuous increase outside the bottom 26, is not specific as the second collection / reinforcement biaxial guide vacant to accommodate the screw cap room is substantially 16 (by the bottle & benzine type bottom, ring part Or convex edge for smooth transition as shown in the figure, pay attention to because of vt first reading-Item% This π is printed by the Ministry of Economic Affairs + Central Standards Bureau Cooperative Society 5i, and the plane extension ratio is about 10: 1. The plane extension is average The ratio of the thickness of the side wall of the bottle. The bulk density bottle is better than the flat extension. The ring extension is 3 _ 3.6: 1 and has a high copolymer core layer 30. In a specific example, 1.5 g, (most Width) The diameter of the inner layer 32 and the outer layer 34 is about 3.6 inches (0.024 inches in diameter). The thickness of the sidewall of the prototype is about 0.230 inches. The stretch ratio is based on the average thickness of the sidewall of the prototype. The thickness of the polyester is about 0.5 ~ 2.0 liters. 1, 8-10: 1 is better, and the shaft extension is 2-3: 1. This provides the container side wall with the required abuse resistance, while the prototype side wall has the required visual transparency. Side wall thickness and selected extension ratio , Depending on the size of the characteristic bottle, internal pressure (for example, beer is 2.0 atm, and soft food is 4 atm ~ 6 ^, wood paper side with the scales in a Η house standard half (CHS) TM Imitating (210x297 well; IT)
HI. 7. 20.00〇ikOD 經濟部屮央標準局β工消伢合作社印3i Λ 6 21-0^-- 五、發明説明(7) ,和特殊材料的加工特性(例如由固有粘度決定)而異。 橫越容器側壁達成的結晶度如第2圖所示。結晶度百 分比依照ASTM 1505決定如下: 結晶度 % =〔(ds — da ) / ( dc - da )〕X 100 其中ds=樣品密度,g/cm3,da = 0 %結晶度的無晶形膜密 度(對PET而言,爲1 . 333 g/CTi3 ),而dc=由單位晶格參 變數計算而得之結晶密度(對PET而言,爲1 . 45 5 g/CTi3 )。 如第2圖所示,頸部12跨越芯層.、內層和外層的結晶 度極低(〇 — 2%),因爲瓶此部份實質上不會膨脹。膨 脹較胴段16爲小的斜肩部丨4,在芯層達15 — 17 %應變引起 的結晶度,而內層和外層爲22 — 24 %應變引起的結晶度。 在高度延伸的胴段16,芯層爲16 _ 18 %應變引起的結晶度 ,內層和外層爲22 — 25 %。較流道20的較厚段和較不會膨 脹的底凹部22,在芯層以及內層和外層又是〇 — 2 %應變 引起的結晶度。在凸邊區24,芯層產生4 _ 8 %的應變引 起結晶度,而內層和外層爲16 — 18 %。另外,利用加熱定 型(熱引起),或合倂應變引起和熱引起的結晶,可達成 不同程度的結晶度。一般而言,應變引起的結晶度傾向於 實質上均勻跨越特定層的厚度,而熱引起的結晶度可顯示 跨越壁的梯度。在本發明中,單只側壁表面的高水準結晶 度即夠,雖然,典型上跨越各層可達成實質上一定平均水 準的結晶度。 吹氣容器基於前述結晶度百分比,實質上應具透明性 。透明性另一量度是發射光透過壁的渾濁百分比(%),定 (請先wl-ift背而.^注意务項再艰寫本頁) 裝. 訂_ 線· 本紙张尺羊边用中a困家《準(CNS) 执怙(210><297公;«:> 81. 7. 20.000张(II) 經濟部屮央標準局β工消作合作社印3i 五、發明説明(8 ) 義如下式: HT =〔Yd+( Yd + Ys )〕X 1〇〇 其中,Yd是樣品所透射的擴散光,Ys是樣品所透射的反射 光。擴散和反射光的透射値是按照ASTM法D 1003測量’ 使用任何標準比色計,諸如Hunterlab,Inc.製造的D25D3P型 。重塡容器的(透壁)渾濁百分比應低於約15 %,以低於 約10 %爲佳,而以低於約5 %更佳。 形成芯層30的高共聚物PET宜含約總重量4— 6%的 共聚單體,諸如1,4 一環己烷二甲醇(CHDM)和/或異苯 二甲酸(IPA)。內層32和外層34用低共聚物PET,宜含約 總重量0 — 2%的共聚單體,諸如CHDM和/或IPA。此 等材料美國田納西州Kingsport市的伊士曼化學公司和俄荄 俄州Akron市的固特異輪胎橡膠公司有售。共聚單體(例 如,CHDM代替二醇部份,或IPA代替酸部份)間斷PET 聚合物架構(即酸和二醇的輪流單元)降低分子結晶率。 共聚單體形成架構的一部份時最具成效,但亦可形成支鏈 共聚物。 __ 瓶最好經二階段雛型射出和隨後的再熱吹氣法製成。 一般而言,瓶(在適溫)受到延伸的部份,顯示跨越側壁 的最大量結晶度。此外,共聚物在多層側壁的不同程度( 見第3圖),產生結晶度的變化,高共聚物芯層30顯示結 晶度較低共聚物內層32和外層34爲低。因在指定溫度提高 共聚物含量,會降低分子結晶率。 結晶率的一項量度,是自差示掃描量熱計(DSC)所得 〜8〜 (請先閲誚背而.5-江意妒項#项寫木頁) 裝- _ 線· 本紙张尺度逍用中8 Η家槔準(CNS) TM规格(2丨0X297公¢) 81. 7. 20.000张(II) 經濟部屮央標準局!3:工消讣合作杜印製 010975_____- 五、發明説明(9) 結晶曲綫,測量ΔΤ ,即ΔΤ = Tie — Τρ,其中Τρ爲結晶 峯部溫度,' 爲初期結晶溫度(開始),而Tie是在放熱 峯部高溫側的切綫對基錢交叉所得外插初期溫度。此項技 術詳載於 H.N. Beck 和 H.D. Ledbetter, J. Appl. Polym. Sci., _^,2131(1965),和3&1611八.>531411:「樹脂和製法參變數 影响PET雛型之結晶化」,BEV-PAK,九二年第十六届飮 料包裝國際Ryder會議,1992年3月23 — 25日,第6 —‘11 圖,全文於此列入參玫。ΔΤ量爲全體結晶率之函數, △T愈小,結晶率愈大。對PET而言,高共聚物一般視爲 AT (以5。(: /分鐘的冷却率,自300 °C至Tg ( 80 °C )以 下而測得)在21.5。(:和以上,而低共聚物在21.5 °C以下。 本發明高、低共聚物層間的ΔΤ差異至少約20 %,例如高 共聚物ΔΤ約24,而低共聚物ΔΤ約20。 吹製瓶所用的雛型,實質上爲非晶形,對PET意指至 約10 %結晶度,以不超過約5 %結晶度爲佳,而以不超過 約2 %更佳。 另外,雛型的實質上非晶形或透明性質,可由渾濁百 分比測定。跨越雛型壁的渾濁百分比應不超過約20 %,以 不超過約10%爲佳,而以不超過約5%更佳。 實質上非晶形雛型即膨脹,在容:器側壁產生配向性和結 晶。可以渉及雛型擴張的任何習知技術,諸如眞空或加壓 成型,將雛型膨脹成容器。二項已知製法是積合射出吹氣 法,以及二段式雛型射出和隨後再熱吹氣法。 擴張步驟應在所用聚酯材料的分子配向溫度範圍內進 本紙张尺度边用中a Η家樣毕(CNS)T4規«5(210X297公;Jt) 8丨.7. 20,000张(II) (請先閲讀背而之'注意市、項孙堝寫本頁) 裝- 線· 21097ο Λ 6 η 6 五、發明説明(10) 行。一般而言,可配向之熱塑 高於玻璃轉化溫度(聚合物 窄溫度範圍)至正好低於聚 生。按實際情況,配向之容器 行,稱爲分子配向溫度範圍 轉化溫度時,材料太硬,無 。當溫度上升,加工性大爲 近開始形成所謂球體之微晶 程受到球體成長的不良影响 而言,分子配向範圍典型上 約 20 至 65 °F ( 11 至 36 °C ), 佳。典型的無晶形PET聚合 ,是在正好 或以下的狹 度範圍內發 度範圍內進 太接近玻璃 設備內延伸 限到達或接 因爲配向過 形聚酯材料 璃轉化溫度 至22 °C )爲 度約168 T )至約205HI. 7. 20.00〇ikOD The Ministry of Economic Affairs, Bureau of Standards, Beta Engineering Cooperative Cooperative Printed 3i Λ 6 21-0 ^-V. Description of the invention (7), and the processing characteristics of special materials (eg determined by intrinsic viscosity) different. The crystallinity achieved across the side walls of the container is shown in Figure 2. The percentage of crystallinity is determined according to ASTM 1505 as follows: Crystallinity% = [(ds — da) / (dc-da)] X 100 where ds = sample density, g / cm3, da = 0% crystallinity of the amorphous film ( For PET, it is 1.333 g / CTi3), and dc = the crystal density calculated from the unit lattice parameter (for PET, it is 1.45 5 g / CTi3). As shown in Figure 2, the neck 12 crosses the core layer. The inner and outer layers have very low crystallinity (0-2%) because this part of the bottle does not substantially swell. The swelling is smaller than the carcass section 16 as a sloping shoulder 丨 4, and the crystallinity caused by 15-17% strain in the core layer, and the crystallinity caused by 22-24% strain in the inner layer and the outer layer. In the highly extended carcass section 16, the core layer is 16-18% strain-induced crystallinity, and the inner and outer layers are 22-25%. The thicker section of the runner 20 and the bottom recess 22 which is less swellable are again crystallinity caused by 0-2% strain in the core layer and the inner and outer layers. In the flange region 24, the core layer produces 4-8% strain to cause crystallinity, while the inner and outer layers are 16-18%. In addition, different degrees of crystallinity can be achieved by heating (heat-induced), or crystallization caused by combined strain and heat. In general, strain-induced crystallinity tends to be substantially uniform across the thickness of a particular layer, while thermally-induced crystallinity can show a gradient across walls. In the present invention, a high level of crystallinity on the surface of a single sidewall is sufficient, although, typically, a crystallinity of substantially a certain average level can be achieved across layers. The blower container should be substantially transparent based on the aforementioned percentage of crystallinity. Another measure of transparency is the percentage of turbidity (%) of the emitted light through the wall, fixed (please refer to wl-ift first. ^ Please pay attention to the items and write this page hard). Binding. Thread a Sleepy family "quasi (CNS) executive (210> < 297 public;«: > 81. 7. 20.000 sheets (II) printed by the Ministry of Economic Affairs, Bureau of Standards, β-consumer cooperative cooperative 3i V. Description of invention (8 ) The meaning is as follows: HT = [Yd + (Yd + Ys)] X 100. where Yd is the diffused light transmitted by the sample and Ys is the reflected light transmitted by the sample. The transmission values of the diffused and reflected light are in accordance with the ASTM method D 1003 measurement 'Use any standard colorimeter, such as Model D25D3P manufactured by Hunterlab, Inc. The (turbid wall) turbidity percentage of heavy tanks should be less than about 15%, preferably less than about 10%, and lower Preferably it is about 5%. The high copolymer PET forming the core layer 30 preferably contains about 4-6% of the total weight of comonomers, such as 1,4-cyclohexanedimethanol (CHDM) and / or isophthalic acid ( IPA). The inner layer 32 and the outer layer 34 are made of low copolymer PET, preferably containing about 0-2% of the total weight of comonomers, such as CHDM and / or IPA. These materials are in Kingsport, Tennessee, USA Are available from Eastman Chemical Company and Goodyear Tire & Rubber Company in Akron, Oregon. Co-monomers (eg, CHDM instead of diol part, or IPA instead of acid part) intermittent PET polymer architecture (ie acid Rotating unit with glycol) reduces the molecular crystallization rate. The comonomer is the most effective when forming a part of the framework, but it can also form a branched copolymer. __ The bottle is best injected through a two-stage prototype and subsequent reheat It is made by blowing. Generally speaking, the part of the bottle (at moderate temperature) that is stretched shows the maximum amount of crystallinity across the side wall. In addition, the copolymer has varying degrees of multi-layer side wall (see Figure 3), resulting in crystallization The degree of change in the high copolymer core layer 30 shows that the lower crystallinity of the copolymer inner layer 32 and the outer layer 34 is low. Because increasing the copolymer content at a specified temperature will reduce the molecular crystallization rate. A measure of the crystallization rate is from Differential Scanning Calorimeter (DSC) obtained ~ 8 ~ (please read the back first. 5- 江 意 闺 项 #Item write a wooden page) installed-_ line CNS) TM specifications (2 丨 0X297cm) 81. 7. 20.000 sheets (II) Ministry of Economic Affairs Bureau of Standards 3: Cooperate with Industrial Consumers to produce 010975 _____- V. Description of the invention (9) Crystallization curve, measure ΔΤ, ie ΔΤ = Tie — Τρ, where Τρ is the crystallization peak temperature, 'is the initial crystallization temperature (start) , And Tie is the initial temperature extrapolated from the tangent to the base cross at the high temperature side of the exothermic peak. This technique is detailed in HN Beck and HD Ledbetter, J. Appl. Polym. Sci., _ ^, 2131 (1965 ), And 3 & 1611 VIII. ≫ 531411: "Resin and manufacturing process parametric variables affect the crystallization of PET prototypes", BEV-PAK, 1992 The 16th International Ryder Conference on Packaging Materials, March 23, 1992 — On the 25th, from the 6th to the 11th, the full text is listed here. The amount of ΔΤ is a function of the overall crystallization rate. The smaller the ΔT, the greater the crystallization rate. For PET, high copolymers are generally regarded as AT (measured at a cooling rate of 5. (: / min, measured from 300 ° C to below Tg (80 ° C)) at 21.5. (: And above, and low The copolymer is below 21.5 ° C. The ΔT difference between the high and low copolymer layers of the present invention is at least about 20%, for example, the high copolymer ΔT is about 24, and the low copolymer ΔT is about 20. The prototype used for blowing bottles is essentially It is amorphous, meaning to PET about 10% crystallinity, preferably not more than about 5% crystallinity, and preferably not more than about 2% crystallinity. In addition, the substantially amorphous or transparent nature of the prototype is Determination of the percentage of turbidity. The percentage of turbidity across the prototype wall should not exceed about 20%, preferably not more than about 10%, and preferably not more than about 5%. In essence, the amorphous prototype expands, in the container: The side walls produce alignment and crystallization. Any conventional technology that can involve the expansion of the prototype, such as emptiness or press molding, expands the prototype into a container. The two known methods are the integrated injection blow method and the two-stage prototype Injection and subsequent hot air blowing. The expansion step should be at the molecular alignment temperature of the polyester material used Within the scope of the paper, the paper is used in the edge of a Η family sample (CNS) T4 regulation «5 (210X297 public; Jt) 8 丨 7.7. 20,000 sheets (II) (please read the back of the words, pay attention to the city, Xiang Sun (This page is written on the crucible). Installation-Line · 21097ο Λ 6 η 6 5. Description of the invention (10) OK. Generally speaking, the thermoplastic that can be oriented is higher than the glass transition temperature (narrow temperature range of the polymer) to just below the polymerization .According to the actual situation, the orientation of the container row, called the molecular alignment temperature range conversion temperature, the material is too hard, no. When the temperature rises, the processability is much closer to the formation of the so-called sphere. The molecular alignment range is typically about 20 to 65 ° F (11 to 36 ° C), which is good. Typical amorphous PET polymerizations extend within a narrow range of just below or extend too close to the glass equipment. Limit to reach or connect because the transition temperature of the over-shaped polyester material glass to 22 ° C) is about 168 T) to about 205
性材料的分 呈玻璃狀態 合物融化溫 的形成是在 。理由是, 法在習知加 改善,但實 大凝聚體的 。對於實質 高於聚酯材 以約30至40 物,其玻璃 圍約195 "FThe material is in a glass state. The melting temperature of the compound is formed. The reason is that the law is improved in knowledge, but it is really agglomerated. For materials that are substantially higher than polyester materials, about 30 to 40, the glass circumference is about 195 " F
子配向 的溫度 度之溫 更狹溫 當溫度 工處理 際的上 溫度, 上非晶 料的玻 °F ( 17 轉化溫 C 91 °C 先 閲 背 而 之 注 意 項 % 木一 頁 裝 玎 線 經濟部屮央榣準历员工消赀合作社印製 (76 °C ) * °F ( % ·<: ) ° 在較佳再 冷至室溫,再 以內。再熱雛 雛型開口端內 的底部,因而 媒質通過桿內 延伸,以符模 和壁厚而異, 而加以控制。 在變通的 般配向溫度範 熱延伸 將雛型 型位於 ,並伸 將雛型 通孔或 具的內 並藉附 吹氣法 在擴張 延伸吹 出抽拉 側壁軸 繞桿進 表面。 加初期 整合製法中 中,熱射出雛型是在使用前驟 步驟之前再熱至配向溫度範圍 氣總成內,其中,延伸桿移入 雛型末端,抵住內腔吹氣模具 向延伸,同時或依序容許吹氣 入雛型內部,將雛型朝外徑向 延伸程度視吹氣容器所需形狀 雛型和完成容器的相對尺寸, 熱射出雛型經部份驟冷,在利 10〜 本紙張尺度边用中S B家ttlMCNS) Ή规怙(2丨0x297公;《:) 81. 7 . 20.000<k(ll) 2 2 經 濟 部 屮 央 標 準 局 貝 工 消 合 作 社 印 31 五、發明説明(11) 用類似前述的適當吹氣或合併延伸/吹氣裝置擴張之前’ 容許其在配向溫度範圍內加以平衡。 第4 一 6圖表示計量的依序共射出裝置,以製造本發 明多層雛型。此裝置實質上如Krishnakumar等人於1987年12 月1日獲准之美國專利4710118號,於此列入參玫。 如第4圖所示,射出模具單元40包含外模腔42,形成 頸部之頸環44,以及芯部46。頸環44聯合芯部46封閉模‘‘腔 42的上端,而下端設有開口 48,以密封關係接受壓出機的 旋轉閥構件52之噴嘴狀末端50。閥構件52以密封關係安裝 於閥塊54內,其中形成第一通道56,容納可塑劑之習知噴 嘴60或射出模頭。通道56徑向通至旋轉閥構件52,後者有 貫穿通道62,一端終至於一般徑向通道64,可與通道56對 準。又與閥塊54相關的是第二材料耗用器66,含有耗用活 塞68,和自此出到閥塊54的流動通道70。閥塊54有徑向通 道72,與通道70軸向通準並相通。閥構件52有另一通道74 ,一般自通道62徑向伸出,沿周與通道64隔開,使得通道 64與通道56對準時,通道74與通道72隔開。轉動閥構件52 ,通道64即移至不與通道56相通,而通道74移至與通道72 相通。因此,可以選擇由第一供應裝置(射出模頭)60或 第二供應裝置66供應材料。 按照較佳具體例,第一供應裝置60輸送的材料爲內層 和外層用低共聚物PET。第二供應裝置砧供應的材料爲芯 層用高共聚物PET。 參見第5圖,可見預選定量的第一低共聚物樹脂76可 〜11〜 本紙張尺度逍用中BH家«^(CNS)T4規怙(2丨0X297公;«:) 81. 7. 20·000张(Π) (請先閲ift背而1注意庐項孙艰窍本頁) 裝· 線- *'· 經濟部屮央櫺準局貝工消ft··合作社印52. 五、發明説明(12) 射入模腔42底部,而在其流經模腔時,由於包含芯部46的 模具單元40溫度較冷,樹脂76會凝固,而形成第一材料的 外表內層78和外層80。 如第6圖簡示,高共聚物芯材86接着射入模腔內。可 見芯材86以隧道式流經二層78、80間限定的腔部,同時把 先前射出材料76向前推。內部芯材冷却較慢,因爲不會接 觸到較冷的模壁,但因芯層具有較高共聚物含量,可抵’抗 渾濁。 參見第7圖,按前述製成雛型110,包含高共聚物芯 層130,連續性低共聚物內層132,和低共聚物外層134 ,除在流道區120延伸穿過外層的一部份芯材外,呈連續 性。雛型110包含上頸部112,自頂到底遞增厚度之斜肩 形成段114,具有均勻壁厚之胴部形成段116,以及底部 形成段118,包含厚度較胴段116爲大之上部,和隣接厚 度縮小之流道區120的下部119。具有較佳重塡應用之斷 面的雛型,載於1991年11月19日准予Krishnakumar等人的美 國專利5066528號,於此全份列入參玫。胴段116的芯層 130大致爲各內層132和外層134厚度的二倍,形成較佳 1.5公升瓶,具有前述壁厚。 如第8圖所述,吹氣容器具有香檳瓶型底段150,包 含流道部152、內凹部154、凸邊156、和外部158。芯 層160以及內層162和外層164,厚度沿底部而異,視特 定底部進行延伸的相對量而定,惟一般而言,隨徑向離開 流道區152,而壁厚遂漸遞減。 12 (請先閱-ift背而之注意带項#褀寫本頁) 裝· ^•- 本紙張尺羊边用中a B家楳準(CNS) ΤΊ执格(210x297公*) 81. 7. 20.000张(II) A 6 n 6 2109^ 五、發明説明(13) 第9圖表示雛型底部形成段218的變通具體例,其中 ,低共聚合材料的第三次射出是射進底部形成段的至少一 部份236,最好是射入縮小壁厚之較低底部219,因其較 薄,冷却較快,不易渾濁。低共聚物段236取代芯材230 ,最好與內層232和外層234的材料相同,故在前述共射 出法中,在次一雛型開始之前,噴嘴清除高共聚物,以免 在次一雛型內,於內層和外層射入任何高共聚物。如第10 圖所示,由第9圖雛型吹製的香檳型容器底部2 50,包含 流道部252 、內凹部254、凸邊256、和外底部258。底 部跨越壁部包含內層262和外層264,以及芯層260。芯 層260在跨越流道和凹部區之段266,至少部份被低共聚 物所取代。 本發明所用熱塑性聚酷材料,最好是基於聚對苯二甲 酸烷二酯(例如乙二酯)(PET)。PET聚合物一般係由對 苯二甲酸或其酯形成性衍生物,與乙二醇或其酯形成性衍 生物製成,包括下式之重複對苯二甲酸乙二酯基: (請先閱請背而之注意枣項#项寫本頁)The temperature of the sub-alignment temperature is narrower. When the temperature is the upper temperature of the process, the glass temperature of the amorphous material is ° F (17 conversion temperature C 91 ° C. Read the back first and pay attention to the items. Printed by the Ministry of Health, Ministry of Health, and Employee Consultation Cooperatives (76 ° C) * ° F (% · <:) ° It is better to cool to room temperature again, then within. Reheat the bottom inside the open end of the prototype Therefore, the medium is extended through the rod, and it is controlled according to the sign and wall thickness. The extension of the normal temperature range in the general orientation will place the prototype model and extend the inside of the prototype through hole or tool. The air blowing method expands and extends the drawing side wall axis around the rod into the surface. In the initial integrated manufacturing method, the hot injection prototype is reheated into the alignment temperature range gas assembly before the use of the previous step, in which the extension rod moves At the end of the prototype, the blow mold of the inner cavity is extended toward the inner cavity, and at the same time or in sequence, the blow is allowed to enter the inside of the prototype, and the radial extension of the prototype is based on the shape of the blow container and the relative size of the completed container. , The hot shot is partly quenched,利 10〜 This paper is used for the standard SB family ttlMCNS) Ή regulations (2 丨 0x297 g; ":) 81.7. 20.000 < k (ll) 2 2 Printed by Beigongxiao Cooperative Society, Bureau of Standards, Ministry of Economic Affairs 31 V. Description of the invention (11) Before expanding with appropriate blowing similar to the aforementioned or the combined extension / blowing device, allow it to be balanced within the range of the alignment temperature. Figures 4 to 6 show the metering sequential co-injection device to manufacture the multilayer prototype of the present invention. This device is essentially US Patent No. 4,710,118, granted by Krishnakumar et al. On December 1, 1987, and is incorporated herein by reference. As shown in FIG. 4, the injection mold unit 40 includes an outer mold cavity 42, a neck ring 44 forming a neck, and a core 46. The neck ring 44 and the core 46 close the upper end of the mold cavity 42 and the lower end is provided with an opening 48 to receive the nozzle-like end 50 of the rotary valve member 52 of the extruder in a sealed relationship. The valve member 52 is installed in the valve block 54 in a sealed relationship, in which a first passage 56 is formed to receive a conventional nozzle 60 of plasticizer or an injection die. The passage 56 opens radially to the rotary valve member 52, the latter having a through passage 62 with one end ending in a general radial passage 64, which can be aligned with the passage 56. Also associated with the valve block 54 is a second material consumer 66, which contains a consumer piston 68, and a flow passage 70 from there to the valve block 54. The valve block 54 has a radial passage 72 which is axially aligned with and communicates with the passage 70. The valve member 52 has another passage 74 that generally extends radially from the passage 62 and is spaced circumferentially from the passage 64 so that when the passage 64 is aligned with the passage 56, the passage 74 is separated from the passage 72. Turning the valve member 52, the channel 64 is moved out of communication with the channel 56, and the channel 74 is moved into communication with the channel 72. Therefore, it is possible to select the first supply device (injection die) 60 or the second supply device 66 to supply the material. According to a preferred embodiment, the material supplied by the first supply device 60 is a low copolymer PET for inner and outer layers. The material supplied by the anvil of the second supply device is a high-copolymer PET for the core layer. Referring to FIG. 5, it can be seen that the pre-selected amount of the first low copolymer resin 76 may be ~ 11 ~ The BH home «^ (CNS) T4 regulation (2 丨 0X297 public;« :) 81. 7. 20 · 000 sheets (Π) (please read ift back first and pay attention to Lu Xiangsun's hardship page) Installed · Line-* '· Ministry of Economic Affairs, Pentagon Bureau of the Ministry of Economic Affairs Bei Gongxiao ft. · Cooperative Printed 52. V. Inventions Explanation (12) When it is injected into the bottom of the cavity 42, and when it flows through the cavity, the mold unit 40 including the core 46 is colder in temperature, and the resin 76 will solidify, forming the outer surface inner layer 78 and the outer layer of the first material 80. As shown briefly in Figure 6, the high copolymer core material 86 is then injected into the mold cavity. It can be seen that the core material 86 flows through the cavity defined between the two layers 78, 80 in a tunnel manner while pushing the previously injected material 76 forward. The internal core material cools slowly because it does not touch the colder mold wall, but because the core layer has a higher copolymer content, it can resist turbidity. Referring to FIG. 7, the prototype 110 is formed as described above, and includes a high copolymer core layer 130, a continuous low copolymer inner layer 132, and a low copolymer outer layer 134, except for a portion extending through the outer layer in the runner region 120 The core material is continuous. The prototype 110 includes an upper neck 112, a sloping shoulder forming section 114 of increasing thickness from top to bottom, a carcass forming section 116 having a uniform wall thickness, and a bottom forming section 118, including a larger upper portion than the carcass section 116, and Adjacent to the lower portion 119 of the flow channel area 120 of reduced thickness. The prototype with better cross-section is contained in U.S. Patent No. 5066528 granted to Krishnakumar et al. On November 19, 1991, and is fully incorporated in Shenmei. The core layer 130 of the carcass section 116 is approximately twice the thickness of each inner layer 132 and outer layer 134, forming a preferably 1.5 liter bottle with the aforementioned wall thickness. As shown in FIG. 8, the air blowing container has a champagne bottle-shaped bottom section 150, and includes a flow channel portion 152, an inner concave portion 154, a flange 156, and an outer portion 158. The thickness of the core layer 160 and the inner layer 162 and the outer layer 164 vary along the bottom, depending on the relative amount of extension of the specific bottom, but generally speaking, the wall thickness gradually decreases as it leaves the flow channel region 152 in the radial direction. 12 (please read the first -ift and note the item #write this page) 装 · ^ •-This paper is used in the edge of the sheep a B Jiayu standard (CNS) ΤΊ 执 格 (210x297 公 *) 81. 7 . 20.000 sheets (II) A 6 n 6 2109 ^ V. Description of the invention (13) FIG. 9 shows a modified specific example of the bottom forming section 218, in which the third injection of the low-copolymer material is the bottom forming At least a portion 236 of the segment is preferably injected into the lower bottom 219 of reduced wall thickness because it is thinner, cools faster, and is less turbid. The low copolymer segment 236 replaces the core material 230, preferably the same material as the inner layer 232 and the outer layer 234, so in the aforementioned co-injection method, before the start of the next prototype, the nozzle clears the high copolymer to avoid the next copolymer In the mold, any high copolymer is injected into the inner and outer layers. As shown in FIG. 10, the champagne-shaped container bottom 250 blown from the prototype of FIG. 9 includes a flow channel portion 252, an inner concave portion 254, a flange 256, and an outer bottom portion 258. The bottom spanning wall includes an inner layer 262 and an outer layer 264, and a core layer 260. The core layer 260 is at least partially replaced by oligomers in the section 266 spanning the flow channel and the recessed area. The thermoplastic polymer material used in the present invention is preferably based on polyalkylene terephthalate (e.g. ethylene glycol) (PET). PET polymers are generally made of terephthalic acid or its ester-forming derivatives, and ethylene glycol or its ester-forming derivatives, including repeating ethylene terephthalate groups of the following formula: (Please read first Please pay attention to Zao item # item write this page)
TT
經濟部屮央榣準局C5工消作合作社印32. 本發明構想使用聚對苯二甲酸乙二酯之共聚物,內有 少量,例如約10 %重量以下的對苯二甲酸乙二酯單元,被 相容性單體單元所取代,其中單體的二醇部份則改爲脂肪 族或脂環族二醇類,諸如環己烷二甲醇、丙二醇、聚丁二 醇、己二醇、十二烷二醇、二乙二醇、聚乙二醇、聚丙二 〜13〜 81. 7. 20.000张(II) 本紙ft尺度逍用肀a S家樣毕(CNS) ΤΊ执怙(210乂297公度} Λ 6 η 6 21〇^° 五、發明説明(w) 醇、丙二醇一1,3、丁二醇~1,4,和新戊二醇、聯酚, 及其他芳香族二醇類,諸如氫醗,以及2,2 —双(4,一 /7 一羥乙氧基苯基)丙烷。可取代於單體單元的二羧酸部份 ,例如包含芳香族二竣酸,諸如異苯二甲酸、苯二甲酸、 萘二羧酸、二苯基二羧酸、二苯氧基乙烷二羧酸、二苯甲 酸,還有脂肪族或脂環族二羧酸,諸如己二酸、癸二酸、 壬二酸、癸烷二羧酸和環己烷二羧酸。此外,各種多官‘能 性化合物,諸如三羥甲基丙烷、季戊四醇、苯偏三酸和苯 均三酸,可與聚對苯二甲酸乙二酯共聚合,其量可在約2 %重量以下。 本發明可用之聚對苯二甲酸乙二酯亦可含有其他相容 性添加劑和成份,對容器的效能特性,諸如對所包裝產品 的味道或其他性能沒有不良影响。此種成份之例包含熱安 定劑、光安定劑、染料、顏料、可塑劑、塡料、抗氧化劑 、潤滑劑、壓出助劑、殘餘單體淨化劑等。 固有粘度(I .V.)影响聚酯樹脂的加工性。製造本發明 容器所用出發材料,可採用固有粘度約0.55至約1.04,最 好約0.55至0.85之聚對苯二甲酸乙二酯。固有粘度是按照 ASTM D-2857程序,採用30 °C溶劑(包括融點〇。<:的隣氯 酚)內0.0050 ± 0.0002 g/me聚合物,加以測量。固有粘度 (I.V.)由下式決定:Printed by C5 Gongxiaozuo Cooperative of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs. 32. The present invention contemplates the use of polyethylene terephthalate copolymers with a small amount, such as about 10% by weight of ethylene terephthalate units. , Replaced by compatible monomer units, where the diol portion of the monomer is changed to aliphatic or cycloaliphatic diols, such as cyclohexanedimethanol, propylene glycol, polybutylene glycol, hexanediol, Dodecanediol, diethylene glycol, polyethylene glycol, polypropylene di ~ 13 ~ 81. 7. 20.000 sheets (II) ft scale of this paper xiao sang a S home sample Bi (CNS) ΤΊ executive (210 乂297 degrees) Λ 6 η 6 21〇 ^ ° V. Description of the invention (w) Alcohol, propylene glycol 1,3, butanediol ~ 1,4, and neopentyl glycol, biphenol, and other aromatic diols Classes, such as hydrazone, and 2,2-bis (4, one / 7-hydroxyethoxyphenyl) propane. The dicarboxylic acid moieties that can be substituted in the monomer unit include, for example, aromatic diacids, such as Isophthalic acid, phthalic acid, naphthalene dicarboxylic acid, diphenyl dicarboxylic acid, diphenoxyethane dicarboxylic acid, dibenzoic acid, and aliphatic or cycloaliphatic dicarboxylic acids, such as hexyl Acids, sebacic acid, azelaic acid, decane dicarboxylic acid and cyclohexane dicarboxylic acid. In addition, various multi-functional compounds, such as trimethylolpropane, pentaerythritol, trimellitic acid and benzene are three Acid, which can be copolymerized with polyethylene terephthalate, the amount of which can be less than about 2% by weight. The polyethylene terephthalate usable in the present invention may also contain other compatible additives and ingredients. Performance characteristics, such as no adverse effects on the taste or other properties of the packaged products. Examples of such ingredients include heat stabilizers, light stabilizers, dyes, pigments, plasticizers, base materials, antioxidants, lubricants, extruded Auxiliaries, residual monomer purification agents, etc. Intrinsic viscosity (I.V.) affects the processability of the polyester resin. The starting material used in the manufacture of the container of the present invention can use an intrinsic viscosity of about 0.55 to about 1.04, preferably about 0.55 to 0.85 Of polyethylene terephthalate. The intrinsic viscosity is in accordance with ASTM D-2857 procedures, using 0.0050 ± 0.0002 g / me polymer in a 30 ° C solvent (including melting point 0. <: o-chlorophenol) Measurement. Intrinsic viscosity (IV) is determined by the following formula set:
I.V. = ( βn ( VsoZn/VsoZ) ) /C 其中:VsoZn爲溶液粘度,以任意單位計 Vso/爲溶劑粘度,以同樣單位計 14 本紙Λ尺度逡用18 B家ttUMCNS) T4执«5(210X297公;tt) (請先wllft背而_之注意-^項#蜞寫本頁)IV = (βn (VsoZn / VsoZ)) / C where: VsoZn is the solution viscosity, in any unit, Vso / is the solvent viscosity, in the same unit, 14 paper Λ scale, 18 B home ttUMCNS) T4 «5 (210X297 Public; tt) (please pay attention to wllft first-^ item #write this page)
T % 經濟部中央標準局貝工消伢合作杜印31 81. 7 . 20.000¾ (II) 2109'Vo 經濟部中央標準而员工消赀合作社印51 五、發明説明(15) C爲每100毫升溶液的聚合 重塡性聚酯飮料瓶生產中的其 年6月15日准予Krishnakimer等人的 1988年2月16日准予Collette的美 及 1991 年 11 月 19 日准予Krishfiakumar 號,均於此全文列入參玫。 如前所述,本發明塑膠容器最 PET )製成。然而,其他熱塑性聚 發明多層容器,其中第一層在射出 熱引起結晶的抵抗性較大,第二層 ,達成較高的應變和/或熱引起的 的表面結晶。除較佳具體例的芯層 設其他層次。可用不同的基材結構 實質上半球形底壁,有複數的向下 持脚爲止,在腿間有橫條(爲底壁 厚、雛型和瓶外形,均因特殊最終 發明物質,容器可供其他加壓或未 酒、果汁或牛奶,或其他非飮料產 如抗渾濁性和提高溫度時的改進抗 用於Collette等人1989年9月5日 號,於此全文列入參玫。熱塡容器 180 — 185 T (產品充塡溫度)之 psi (充塡綫上壓力),而無實質 因此,雖然本發明有若干較佳 〜15〜 物克數之濃度 他重要因數,載於1982 美國專利4334627號, 國專利4725464號,以 等人的美國專利5066528 好由聚對苯二 酯樹脂亦可用 或類熱處理過 在隨後吹氣或 結晶,以提供 、內層和外層 ,諸如有脚基 延伸腿,到最 的一部份)。 產品而異,仍 加壓飮料之用 品。本發明的 應力龜裂性, 獲准的美國專 典型上必須能 譜,而正內壓 變形。 具體例,已如 甲酸酯( 以達成本 程中,對 膨脹階段 較高程度 外,可加 部,具有 下方的支 材料、壁 然加設本 ,諸如啤 益處,例 可特別適 利 4863046 耐升溫至 逹2 — 5 圖示和上 1? 先 閲 讀 背 而 乏 注 意 項 # % 本·> 裝 rr 線 私紙ft尺度边用中S®家標準(CNS)T4規怙(2丨0x297公;Jt) 8K 7. 20,000ik(il) Λ 6 B6 2l〇SsV〇 五、發明説明(16) 述,須知在雛型構造、材料、容器構造和容器形成方法上 均可變化,而不違本發明申請之精神和範圍。 先 閲 in 背 而 之 注 意 事 項 •4 填 % 本 rr 裝 線 經濟部屮央榀準局貝工消卟合作杜印驭 16 本紙张尺度边用中a B家榣準(CNS)T4規怙(2丨0X297公;《:) 81. 7. 20.000ΪΜΙΙ)T% Ministry of Economic Affairs, Central Standards Bureau, Bei Gong Consumer Cooperation Du Yin 31 81. 7. 20.000¾ (II) 2109'Vo Ministry of Economic Affairs Central Standards and Employee Consultation Cooperatives printed 51 V. Description of invention (15) C is for every 100 ml In the production of polymerized heavy-duty polyester urn bottles for solutions, the United States granted Krishnakimer et al. On February 16, 1988 to Collette on February 16, 1988 and the Krishfiakumar number granted on November 19, 1991, both of which are listed here. Enter Shenmei. As mentioned above, the plastic container of the present invention is made of PET). However, in other thermoplastic poly-invented multilayer containers, the first layer is more resistant to crystallization caused by heat injection, and the second layer achieves higher strain and / or heat-induced surface crystallization. In addition to the core layer of the preferred embodiment, other layers are provided. Different base materials can be used. Substantially hemispherical bottom wall, with a plurality of downward holding feet, and horizontal bars between the legs (the bottom wall thickness, prototype and bottle shape, all due to special final invention materials, containers are available Other pressurized or non-alcoholic, fruit juice or milk, or other non-distilled materials such as turbidity resistance and improved resistance at elevated temperatures are used in Collette et al. September 5, 1989, the full text of which is listed in Shenmei. Container 180-185 T (product charging temperature) psi (filling pressure on the line) without substance. Therefore, although the present invention has a number of preferred concentrations of ~ 15 ~ the number of grams of other important factors, contained in the 1982 US patent No. 4334627, National Patent No. 4725464, U.S. Patent No. 5066528, etc. The polyterephthalate resin can also be heat treated or similarly blown or crystallized afterwards to provide, inner and outer layers, such as foot extension legs , To the most part). The product varies, and the product is still pressurized. The stress cracking property of the present invention, the approved U.S. patent must typically be energy spectrum, and the positive internal pressure deformation. Specific examples, such as formate (in the cost process, in addition to the higher degree of expansion stage, can be added, with the following branch materials, wall installation costs, such as beer benefits, examples can be particularly suitable for 4863046 Temperature rises to 2 — 5 Picture and 1 above? First read the back and lack of attention #% This ·> Install rr line private paper ft scale side use S® Home Standard (CNS) T4 regulation (2 丨 0x297 ; Jt) 8K 7. 20,000ik (il) Λ 6 B6 2l〇SsV〇 Fifth, the description of the invention (16) stated that the basic structure, material, container structure and container formation method can be changed without violating the original The spirit and scope of the invention application. First read in Contrary Notes • 4 Fill% This rr is installed by the Ministry of Economic Affairs, the Central Bureau of Economics and Trade, Pinggong Porridge Cooperative, and Du Yinyu. 16 This paper is for standard use. (CNS) T4 regulation (2 丨 0X297 male; ":) 81. 7. 20.000ΪΜΙΙ)
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TW81106831A TW210976B (en) | 1992-07-07 | 1992-08-29 | Multi-layer refillable container having higher wash temperature and redvced product flavor carryover, preform and method of forming same |
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WO1995014761A1 (en) * | 1993-11-22 | 1995-06-01 | Pernod Ricard | Process for washing refillable plastic bottles |
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WO1995014761A1 (en) * | 1993-11-22 | 1995-06-01 | Pernod Ricard | Process for washing refillable plastic bottles |
FR2712828A1 (en) * | 1993-11-22 | 1995-06-02 | Pernod Ricard | Process for washing refillable plastic bottles. |
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