TWI320771B - Article having high barrier property - Google Patents

Article having high barrier property Download PDF

Info

Publication number
TWI320771B
TWI320771B TW094142900A TW94142900A TWI320771B TW I320771 B TWI320771 B TW I320771B TW 094142900 A TW094142900 A TW 094142900A TW 94142900 A TW94142900 A TW 94142900A TW I320771 B TWI320771 B TW I320771B
Authority
TW
Taiwan
Prior art keywords
article
weight
group
clay
ethylene
Prior art date
Application number
TW094142900A
Other languages
Chinese (zh)
Other versions
TW200621871A (en
Inventor
Myung Ho Kim
Minki Kim
Sehyun Kim
Youngtock Oh
Jaeyong Shin
Youngchul Yang
Original Assignee
Lg Chemical Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Lg Chemical Ltd filed Critical Lg Chemical Ltd
Publication of TW200621871A publication Critical patent/TW200621871A/en
Application granted granted Critical
Publication of TWI320771B publication Critical patent/TWI320771B/en

Links

Classifications

    • GPHYSICS
    • G02OPTICS
    • G02FOPTICAL DEVICES OR ARRANGEMENTS FOR THE CONTROL OF LIGHT BY MODIFICATION OF THE OPTICAL PROPERTIES OF THE MEDIA OF THE ELEMENTS INVOLVED THEREIN; NON-LINEAR OPTICS; FREQUENCY-CHANGING OF LIGHT; OPTICAL LOGIC ELEMENTS; OPTICAL ANALOGUE/DIGITAL CONVERTERS
    • G02F1/00Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics
    • G02F1/01Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour 
    • G02F1/13Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on liquid crystals, e.g. single liquid crystal display cells
    • G02F1/133Constructional arrangements; Operation of liquid crystal cells; Circuit arrangements
    • G02F1/1333Constructional arrangements; Manufacturing methods
    • G02F1/1335Structural association of cells with optical devices, e.g. polarisers or reflectors
    • G02F1/1336Illuminating devices
    • G02F1/133615Edge-illuminating devices, i.e. illuminating from the side
    • GPHYSICS
    • G02OPTICS
    • G02BOPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B6/00Light guides; Structural details of arrangements comprising light guides and other optical elements, e.g. couplings
    • G02B6/0001Light guides; Structural details of arrangements comprising light guides and other optical elements, e.g. couplings specially adapted for lighting devices or systems
    • G02B6/0011Light guides; Structural details of arrangements comprising light guides and other optical elements, e.g. couplings specially adapted for lighting devices or systems the light guides being planar or of plate-like form
    • G02B6/0066Light guides; Structural details of arrangements comprising light guides and other optical elements, e.g. couplings specially adapted for lighting devices or systems the light guides being planar or of plate-like form characterised by the light source being coupled to the light guide
    • G02B6/0068Arrangements of plural sources, e.g. multi-colour light sources
    • GPHYSICS
    • G02OPTICS
    • G02BOPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B6/00Light guides; Structural details of arrangements comprising light guides and other optical elements, e.g. couplings
    • G02B6/0001Light guides; Structural details of arrangements comprising light guides and other optical elements, e.g. couplings specially adapted for lighting devices or systems
    • G02B6/0011Light guides; Structural details of arrangements comprising light guides and other optical elements, e.g. couplings specially adapted for lighting devices or systems the light guides being planar or of plate-like form
    • G02B6/0066Light guides; Structural details of arrangements comprising light guides and other optical elements, e.g. couplings specially adapted for lighting devices or systems the light guides being planar or of plate-like form characterised by the light source being coupled to the light guide
    • G02B6/0073Light emitting diode [LED]
    • GPHYSICS
    • G02OPTICS
    • G02FOPTICAL DEVICES OR ARRANGEMENTS FOR THE CONTROL OF LIGHT BY MODIFICATION OF THE OPTICAL PROPERTIES OF THE MEDIA OF THE ELEMENTS INVOLVED THEREIN; NON-LINEAR OPTICS; FREQUENCY-CHANGING OF LIGHT; OPTICAL LOGIC ELEMENTS; OPTICAL ANALOGUE/DIGITAL CONVERTERS
    • G02F2201/00Constructional arrangements not provided for in groups G02F1/00 - G02F7/00
    • G02F2201/52RGB geometrical arrangements

Landscapes

  • Physics & Mathematics (AREA)
  • Optics & Photonics (AREA)
  • General Physics & Mathematics (AREA)
  • Nonlinear Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mathematical Physics (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Containers Having Bodies Formed In One Piece (AREA)
  • Paints Or Removers (AREA)
  • Laminated Bodies (AREA)

Description

1320771 18784pif.doc 九、發明說明: 本申請案主張於2004年12月7號向韓國智慧財產局 ,· 提出申請之韓國專利申請案第10-2004-0102214號以及於 .· 2005年4月22號向韓國智慧財產局提出申請之韓國專利 申請案第10-2005-0033527號的優先權,該專利申請案所 揭露之内容系完整結合於本說明書中。 【發明所屬之技術領域】 本發明係關於具有高阻絕性及具有經一氟塗覆之内壁 • 的物品,其中一插入黏土與一具有阻絕性之樹脂的奈米^ 合物以特定形式分散於聚烯烴樹脂基質中。 又 • 【先前技術】 - 諸如聚乙烯(Polyethylene )及聚丙烯(p〇iypr〇pyIene) 之通用樹脂由於其優良的可塑性、機械性質及濕氣阻絕 性,被用於許多領域中。然而,此等樹脂之使用限於要^ 優良化學及氧阻絕性之農用化學品及食品的包裝或容器。 因此,通用樹脂藉由共擠出、層壓、塗覆等與其他樹脂一 φ 起呈多層用於該等材料之包裝或容器。 由於乙烯-乙烯醇(ethylene_vinyUlc〇h〇1,ev〇h)共 聚物及聚醯胺(P〇iyamide)樹脂之透明性及良好的氣體^且 絕性,其被用於多層塑料產品。然而,因為乙稀_乙稀醇共 ,聚物及聚酸胺樹脂比通用樹脂昂貴,所以即使當使用少量 此等樹脂時,,仍需要具有良好阻絕性之樹脂組合物。 同時’當奈米尺寸的插入黏土與聚合化合物混合而形 成完全剝落、部分贿、插人或部分插人的奈米複合物時, 5 18784pif.doc 由於其形態,其具有改良的阻絕性。因而出現使用此奈书 複合物之具有阻絕性的物品。 不一、 即使在模製後,此對於該奈米複合物維持其完全剝 落、部分剝落、插入或部分插入的形態而言是重要的且完 全剝落形態有利於改良阻絕性。詳言之,當自該奈米複: 物與基質聚合物的組合物製備模製物品時,對於改良阻二 性而言,分散於該基質聚合物中的奈米複合物的形態 重要的。 疋 同時’為改良具有阻絕性之容器中所使用的聚乙歸及 其他聚合物之溶劑與蒸汽阻絕性,常常於模製物品之内壁 上使用氟塗層。於美國專利第2,811,468 A號(J〇ffre)及 美國專利第3,862,284A號(Dixon等人)中揭露此方法。 在美國專利第2,811,468 A號中,首先於室溫下氟化聚^乙 稀,以使其作為周於包裝食品及廢物之枋料具有改良的阻 絶性。在此專利中,亦描述製造吹塑成形之容器的方法, 其中使用反應性含氟流體介質,以使熔融聚乙烯型坯與模 之外形相符。在此方法中,於腔室中,藉由於室溫下用含 氟氣體接觸聚乙烯表面2〇至150分鐘以使氟的濃度為〇.〇3 至3.5重量% (以聚乙烯重量計),來氟化聚乙烯膜及容器 壁。美國專利第3,船,284 A號揭露通過氟化仙生產具有 改良阻絕性之吹塑成形熱塑性物品的方法。在此方法中, 將含有惰性氣體及0.1至10體積%之氟的反應性氣體注入 型坯中’以將該型坯擴展成想要之形狀。注入進行約$秒, 且於高溫下執行。接著,將型坯冷卻以回收反應性氣體並 IJ20771 18784pif.doc 獲得-容器。使用吹塑成形法製造對烴具有良好阻絕性之 燃料槽(市售,商品名為Airopak)。在該方法中,用惰性 氣體擴展型坯,且接著脫氣。此後,將含有〇1至1〇重量 %之氟的反應性氣體注入型坯中,以使型坯形成想要之^ 狀。接著,自型坯移除反應性氣體,且自模移除所得容器( 自從發展了 Dixon等人的高溫吹塑成形法以來,已發展許 多吹塑成形法,且一些於例如美國專利第4,83〇,81〇a號、 美國專利第4,617,077號及美國專利第七869,859中揭露。1320771 18784pif.doc IX. Inventive Note: This application claims to apply to the Korean Intellectual Property Office on December 7, 2004, and to apply for Korean Patent Application No. 10-2004-0102214 and April 22, 2005. The priority of the Korean Patent Application No. 10-2005-0033527 filed by the Korean Intellectual Property Office is hereby incorporated by reference in its entirety. TECHNICAL FIELD OF THE INVENTION The present invention relates to articles having high barrier properties and having a fluorine-coated inner wall, wherein a nano-inserted clay and a resin having a barrier resin are dispersed in a specific form. In a polyolefin resin matrix. Further • [Prior Art] - General-purpose resins such as polyethylene (polyethylene) and polypropylene (p〇iypr〇pyIene) are used in many fields due to their excellent plasticity, mechanical properties and moisture resistance. However, the use of such resins is limited to packaging or containers of agrochemicals and foods that are excellent in chemical and oxygen barrier properties. Therefore, the general-purpose resin is multi-layered for packaging or containers of the materials by co-extrusion, lamination, coating, and the like with other resins. Ethylene-vinyl alcohol (ethylene_vinyUlc〇h〇1, ev〇h) copolymers and polyfluorene (P〇iyamide) resins are used in multilayer plastic products because of their transparency and good gas properties. However, since ethylene-ethyl alcohol co-polymers and polyamine resins are more expensive than general-purpose resins, even when a small amount of these resins are used, a resin composition having good barrier properties is required. At the same time, when a nano-sized insert clay is mixed with a polymeric compound to form a fully flaking, partially bribed, inserted or partially inserted nanocomposite, 5 18784pif.doc has improved barrier properties due to its morphology. Thus, there is a hindrance to the use of this nano-composite. Not all, even after molding, this is important for the morphology of the nanocomposite to maintain its fully exfoliated, partially exfoliated, inserted or partially inserted and the fully exfoliated morphology facilitates improved barrier properties. In particular, when a molded article is prepared from the composition of the nanoparticle and the matrix polymer, the morphology of the nanocomposite dispersed in the matrix polymer is important for improving the barrier properties.疋 At the same time, in order to improve the solvent and vapor barrier properties of polyethylene and other polymers used in barrier-free containers, fluorine coatings are often used on the inner walls of molded articles. This method is disclosed in U.S. Patent No. 2,811,468 A (J. ff.) and U.S. Patent No. 3,862,284 (Dixon et al.). In U.S. Patent No. 2,811,468 A, first, fluorinated polyethylene at room temperature to provide improved resistance as a coating for packaging foods and waste. Also described in this patent is a method of making a blow molded container in which a reactive fluorine-containing fluid medium is used to conform the molten polyethylene parison to the outer shape of the mold. In this method, in the chamber, by contacting the surface of the polyethylene with a fluorine-containing gas at room temperature for 2 to 150 minutes to have a fluorine concentration of 〇.3 to 3.5% by weight (based on the weight of the polyethylene), To fluorinate polyethylene film and container wall. U.S. Patent No. 3, Vessel, No. 284 A discloses the production of a blow molded thermoplastic article having improved barrier properties by fluorinated scent. In this method, a reactive gas containing an inert gas and 0.1 to 10% by volume of fluorine is injected into the parison to expand the parison into a desired shape. The injection is carried out for about $ seconds and is performed at a high temperature. Next, the parison was cooled to recover a reactive gas and a container was obtained by IJ20771 18784 pif.doc. A blow molding method is used to produce a fuel tank (commercially available under the trade name of Airopak) which is excellent in resistance to hydrocarbons. In this method, the parison is expanded with an inert gas and then degassed. Thereafter, a reactive gas containing 1 to 1% by weight of fluorine is injected into the parison to form the parison into a desired shape. Next, the reactive gas is removed from the parison and the resulting container is removed from the mold (a number of blow molding methods have been developed since the development of the high temperature blow molding process by Dixon et al., and some, for example, U.S. Patent No. 4, It is disclosed in U.S. Patent No. 4,617,077 and U.S. Patent No. 7,869,859.

因為塗覆於容器上的氟防止材料穿透,所以該氟塗層可改 良容器之阻絕性。在由聚乙烯製成並用氟塗覆的容^中, 增加塗層之厚度以滿足更嚴格的環境法規。當氟塗^厚度 大時,由於頻繁交換内含物,燃料槽或填充管(其中内含 物頻繁交換)中之氟塗層可經長時間週期被逐漸移除,導 致阻絕性降低。由於此問題變得已知,所以於車輛燃料槽 或填充管中氟塗層的使用顯著減少。 S 【發明内容】 本發明提供具有優良機械強度及優良氧、有機溶劑及 屬氣阻絕性的氟塗覆的物品,其中奈米複合物以特定形式 分散於基質聚合物中,且即使在模製後仍維持其剝落形 態。使用具有良好阻絕性之組合物製造該物品且其具有薄 的氟塗層。由於該物品内壁之良好的阻絕性,即使在釋放 氟塗層時,該物品仍防止内含物滲透及穿透。 根據本發明之一恕樣,本發明提供具有阻絕性及一氟 塗覆之内壁的物品,5亥物品由乾混合組合物製造,該組合 7 爲第94142900號中文說明書無劃線修正頁 18784pif.docSince the fluorine applied to the container prevents the material from penetrating, the fluorine coating can improve the barrier properties of the container. In a container made of polyethylene and coated with fluorine, the thickness of the coating is increased to meet more stringent environmental regulations. When the thickness of the fluorine coating is large, the fluorine coating in the fuel tank or the filling tube (where the contents are frequently exchanged) can be gradually removed over a long period of time due to frequent exchange of the contents, resulting in a decrease in the barrier property. As this problem becomes known, the use of fluorine coatings in vehicle fuel tanks or fill tubes is significantly reduced. S SUMMARY OF THE INVENTION The present invention provides a fluorine coated article having excellent mechanical strength and excellent oxygen, organic solvent and gas barrier properties, wherein the nanocomposite is dispersed in a specific form in a matrix polymer, and even molded. After that, it still maintains its peeling form. The article was made using a composition having good barrier properties and it had a thin fluorine coating. Due to the good barrier properties of the inner wall of the article, the article prevents penetration and penetration of the contents even when the fluorine coating is released. According to one aspect of the present invention, the present invention provides an article having a barrier-resistant and fluorine-coated inner wall, the 5H article being manufactured from a dry mix composition, which is the 94142900 Chinese specification without a sizing correction page 18784pif. Doc

L 物包括:40至96重量份的聚烯烴樹脂;〇·5至60重量份 的具有阻絕性之奈米複合物,該奈米複合物包括一插入黏 土及選自由下列各物組成之群的具有阻絕性的至少一種樹 脂:乙烯·乙烯醇(EVOH)共聚物、聚醯胺、離子聚合物 (ionomer)及聚乙烯醇(p〇lyVinyi alc〇ho卜 PVA);及 1 至30重量份的相容劑。奈米複合物中具有阻絕性之樹脂與 插入黏土的重量比為58.0 : 42.0至99.9 : 0.1。相容劑為選 自由乙烯-乙烯酐-丙烯酸共聚物(ethylene-ethylene anhydride-acrylic acid copolymer)、乙稀-丙烯酸乙酯共聚物 (ethylene-ethyl aery late copolymer )、乙烯-丙烯酸烧基酯-丙浠酸共聚物(ethylene-alkyl acrylate-acrylic acid copolymer)、順丁烯二酸酐改質(接枝)高密度聚乙烯 (maleic anhydride modified (graft) high-density polyethylene)、順丁稀二酸酐改質(接枝)直鏈低密度聚 乙婦(maleic anhydride modified (graft) linear low-density polyethylene)、乙烯-(甲基)丙烯酸炫基酯-(甲基)丙烯 酸共聚物(ethylene-alkyl (meth)acrylate-(meth)acrylic acid copolymer )、己稀-丙晞酸丁醋共聚物(ethylene-butyl acrylate copolymer )、乙烯-乙酸乙稀酯共聚物 (ethylene-vinyl acetate copolymer )、順丁烯二酸針改質(接 枝)乙稀-乙酸乙烯醋共聚物(maleic anhydride modified (graft) ethylene-vinyl acetate copolymer)戶斤組成之族群中之 一或多個化合物。具有阻絕性的物品為容器、膜、管或薄 片。氟塗覆内壁之塗層之厚度為0.02至llym。 1320771 18784pif.doc 根據本發明之另一態樣,本發明提供製造具有阻絕性 之物品的方法,其包括:藉由乾混合40至96重量份的聚 烯烴樹脂、0.5至6〇重量份的具有阻絕性的奈米複合物及 1至3 0重量份的相容劑來製備具有阻絕性的奈米複合物組 合物,該奈米複合物包括一插入黏土及選自由下列各物組 成之群的具有阻絕性的至少一種樹脂:乙烯-乙烯醇 (EVOH )共聚物、聚醯胺、離子聚合物及聚乙烯醇 (PVA);模製該組合物以形成一物品;以及用氟塗覆該模 製物品之一内壁。 在本發明之一實施例中,聚烯烴樹脂可為選自由下列 各物組成之群的至少一種化合物:高密度聚乙烯(high density polyethylene、HDJPE )、低密度聚乙烯(i〇w density poly ethylene、LDPE )、直鏈低密度聚乙稀(unear i〇 w densit》, polyethylene 、LLDPE )、乙烯-丙烯共聚物 (ethylene-propylene copolymer )、茂金屬聚乙稀 (metallocene polyethy丨ene )及聚丙烯。聚丙烯可為選自由 下列各物組成之群之至少一種化合物··丙稀均聚物 (homopolymer of propylene )、丙烯共聚物(c〇p〇lymer 〇f propylene)、戊金屬聚丙烯(metau〇cenep〇iypr〇pyiene)及 藉由向丙烯之均聚物或共聚物添加滑石、阻燃劑等而具有 改良物理性質的複合樹脂。 在本發明之另一實施例中,插入黏土可為選自由下列 各物組成之群的至少一種材料:蒙脫土· (montmorillonite )、膨潤土( bentonite )、高嶺土 9 18784pif.doc (kaolinite)、雲母(mica)、裡皂石(hectorite)、氟化經 皂石(fluorohectorite )' 皂石(saponite )、貝得石(beidelite )、 綠脫石(nontronite ) '石夕鎂石(stevensite )、虫至石 (vermiculite )、多水高嶺土( hallosite )、唯康土 (volkonskoite)、沙康土(suconite)、馬吉土(magadite)以及 肯尼土(kenyalite)。 在本發明之另一實施例中,聚醯胺可為:耐綸4.6、 耐論6、财綸6.6、耐綸6.10、耐綸7、耐綸8、耐綸9、 耐綸11、耐綸12、耐綸46、MXD6、非晶系聚醯胺、含有 至少兩個此等聚醯胺之共聚合聚醯胺或至少兩個此等聚酿 胺之混合物。 在本發明之另一實施例中,離子聚合物可具有每1〇 分鐘〇.1至ίο克之熔融指數(190〇c,2,16〇克)。 在本發明之另一實施例中,可使用高溫吹塑成形法執 行氟塗覆。 【實施方式】 現將更詳細地說明本發明。 由乾混合組合物製備根據本發明之實施例之具有阻絕 性的物品,該組合物包括:40至96重量份的聚婦煙樹脂. 至60重量份之具有阻絕性的奈米複合物,其包括插入 黏土及選自由下列各物域之群的具有轉性的至少一種 樹脂:乙烯-乙稀醇(EV0H)共聚物、聚酿胺、離子聚合 1320771 18784pif.docThe L material comprises: 40 to 96 parts by weight of a polyolefin resin; and 5 to 60 parts by weight of a barrier-resistant nanocomposite comprising an intercalated clay and a group selected from the group consisting of the following: At least one resin having barrier properties: ethylene vinyl alcohol (EVOH) copolymer, polyamine, ionomer, and polyvinyl alcohol (P〇lyVinyi alc〇ho); and 1 to 30 parts by weight Compatibilizer. The weight ratio of the barrier resin to the intercalated clay in the nanocomposite was 58.0: 42.0 to 99.9: 0.1. The compatibilizer is selected from the group consisting of ethylene-ethylene anhydride-acrylic acid copolymer, ethylene-ethyl aery late copolymer, ethylene-acrylic acid alkyl ester-propyl Ethylene-acrylate acrylate-acrylic acid copolymer, maleic anhydride modified (graft) high-density polyethylene, modified by cis-succinic anhydride (graft) linear low-density polyethylene (maleic anhydride modified (graft) linear low-density polyethylene), ethylene-alkyl (meth) acrylate-methacrylic acid (meth) acrylate (meth) Acrylate-(meth)acrylic acid copolymer), ethylene-butyl acrylate copolymer, ethylene-vinyl acetate copolymer, maleic acid needle One or more compounds of the group consisting of the modified (grafted) ethylene-vinyl acetate copolymer. A barrier article is a container, film, tube or sheet. The coating of the inner wall of the fluorine coating has a thickness of 0.02 to 1 lym. 1320771 18784pif.doc According to another aspect of the present invention, there is provided a method of producing an article having barrier properties comprising: by dry mixing 40 to 96 parts by weight of a polyolefin resin, 0.5 to 6 parts by weight of having a barrier nanocomposite and 1 to 30 parts by weight of a compatibilizing agent to prepare a barrier nanocomposite composition comprising an intercalated clay and a group selected from the group consisting of At least one resin having barrier properties: ethylene-vinyl alcohol (EVOH) copolymer, polyamine, ionic polymer, and polyvinyl alcohol (PVA); molding the composition to form an article; and coating the mold with fluorine One of the inner walls of the article. In one embodiment of the present invention, the polyolefin resin may be at least one compound selected from the group consisting of high density polyethylene (HDJPE), low density polyethylene (i〇w density poly ethylene). , LDPE), linear low-density polyethylene (unear i〇w densit, polyethylene, LLDPE), ethylene-propylene copolymer, metallocene polyethy丨ene, and polypropylene . The polypropylene may be at least one compound selected from the group consisting of homopolymer of propylene, propylene copolymer (c〇p〇lymer 〇f propylene), and pentylene metal (metau〇). Cenep〇iypr〇pyiene) and a composite resin having improved physical properties by adding talc, a flame retardant or the like to a homopolymer or copolymer of propylene. In another embodiment of the present invention, the intercalation clay may be at least one material selected from the group consisting of: montmorillonite, bentonite, kaolin 9 18784pif.doc (kaolinite), mica (mica), hectorite, fluorohectorite 'saponite', saponite, beidelite, nontronite 'stevensite', insect to Vermiculite, hallosite, volkonskoite, suconite, magadite, and kenyalite. In another embodiment of the present invention, the polyamidamine can be: nylon 4.6, Nike, 6, 6.6, Nylon 6.10, Nylon 7, Nylon 8, Nylon 9, Nylon 11, Nylon 12. A nylon 46, MXD6, amorphous polyamine, a copolymerized polyamine containing at least two of these polyamines or a mixture of at least two such polyamines. In another embodiment of the invention, the ionic polymer may have a melt index (190 〇 c, 2, 16 gram) per 1 〇 〇.1 to ίο克. In another embodiment of the invention, the fluorine coating can be performed using a high temperature blow molding process. [Embodiment] The present invention will now be described in more detail. A barrier article according to an embodiment of the present invention is prepared from a dry mix composition, the composition comprising: 40 to 96 parts by weight of polyglycol resin. Up to 60 parts by weight of a barrier nanocomposite, The invention comprises inserting clay and at least one resin selected from the group consisting of: ethylene-ethylene glycol (EVOH) copolymer, polyamin, ionic polymerization 1320771 18784pif.doc

種化群的至少- ⑽E)、直鏈低密度聚乙度聚乙烤 物、茂金屬聚㈣及聚_ 1 丙婦共聚 組成之群之至少一種化人:,=烯可為适自由下列各物At least one of the group consisting of at least - (10) E), a linear low-density polyethylene polybide, a metallocene poly(tetra), and a poly- 1-4 copolymerization group: Object

茂金。 •丙烯均聚物、丙烯共聚物、 戊金屬t丙%及猎由向丙烯之均聚物或共 阻燃劑等而具有改良物雜㈣複合魅。’、μ 含量健為4(}至%重量份,且更佳為 重讀。若聚烯域脂之含量小於4G重量份,則 :以成形。若聚晞煙樹月旨之含量大於%重量份,則阻絕性 友0Maojin. • A propylene homopolymer, a propylene copolymer, a pentylene metal, a propanol, a homopolymer or a co-flame retardant to propylene, and the like. ', μ content is healthy 4 (} to % by weight, and more preferably read. If the content of the polyene grease is less than 4G parts by weight: to form. If the content of the poly-smoke tree is greater than % by weight , blocking sexual friend 0

可錯由將一插入黏土與選自由乙烯_乙燥醇(EV〇H) 共聚物、聚醯胺、離子聚合物及聚乙烯醇(pVA)組成之 群的至少一種樹脂混合來製備具有阻絕性的奈米複合物。 所製備之奈米複合物具有完全剝落、部分剝落、插入或部 分插入的形態。 奈米複合物中具有阻絕性之樹脂與插入黏土的重量比 為 58.0 : 42.0 至 99.9 : 0.1,且較佳為 85.0 : 15.0 至 99.0 : 1 ·〇。若具有阻絕性之樹脂與插入黏土的重量比小於58.0 : 42·0 ’則插入黏土聚結且難以分散。若具有阻絕性之樹脂 與插入黏土的重量比大於99.0 : 1.0,則阻絕性的改良是可 忽略的。 1320771 18784pif.doc 插入黏土較佳為有機插入黏土 &插入黏土中有機材料 的含量較佳為1至45重量%。當有機材料的含量小於1重 1%時’插入黏土與具有阻絕性之樹脂的相容性差。當有 機材料的含量大於45重量%時,難以插入具有阻絕性之樹 脂°有機材料具有選自由下列各物組成之群的至少一個官 能基.一級録(primary ammonium )至四級錢(quaternary ammonium )、鱗(phosphonium )、順丁稀二酸酯(maleate )、 破轴酸醋(succinate )、丙烯酸醋(acrylate )、苯甲基氫 (benzylic hydrogen)、σ惡峻味(oxazoline)及二甲基二硬 脂醒錢(dimethyldistearylammonium )。 插入黏土包括選自蒙脫土、膨潤土、高嶺土、雲母、 經皂石、氟化鋰皂石、皂石、貝得石、綠脫石、矽鎂石、 虫至石、多水高嶺土、唯康土、沙康土、馬吉土及肯尼土的 至少一種材料;且有機材料較佳具有選自一級銨至四級 錢、鱗、順丁婦二酸醋、破ίό酸醋、丙烯酸S旨、苯甲基氣、 噁唑啉及二甲基二硬脂醯銨的一個官能基。 若奈米複合物中包括乙烯-乙烯醇共聚物,則該乙歸_ 乙烯醇共聚物中乙稀的含量較佳為10至50莫耳%。若& 烯的含量小於10莫耳%,則由於可加工性差,變得難以炫 融成形。若乙烯的含量超過50莫耳%,則氧及液體阻絕性 不足。 若奈米複合物中包括聚醯胺,則聚醯胺可為: 4.6、耐绘6、耐論· 6.6、而才論6.10、财論7、而才論8u ’ 而才給 9、耐綸11、耐綸12、耐綸46、MXD6、非晶系聚驢胺、 12 1320771 18784pif.doc 含有至少兩個此等聚醯胺之共聚合聚醯胺或至少兩個此等 聚醯胺之混合物。 非晶系聚醯胺指結晶度不足的聚醯胺,意即,當藉由 差示掃描熱量測定(DSC) (ASTM D-3417,l〇°C/分鐘) 量測時,不具有一吸熱結晶熔融峰。It may be prepared by mixing an intercalation clay with at least one resin selected from the group consisting of ethylene-ethyl alcohol (EV〇H) copolymer, polyamidamine, ionic polymer and polyvinyl alcohol (pVA). Nanocomposite. The prepared nanocomposite has a form of complete flaking, partial flaking, insertion or partial insertion. The weight ratio of the barrier resin to the intercalated clay in the nanocomposite is 58.0 : 42.0 to 99.9 : 0.1, and preferably 85.0 : 15.0 to 99.0 : 1 · 〇. If the weight ratio of the barrier resin to the inserted clay is less than 58.0: 42·0 ', the inserted clay coalesces and is difficult to disperse. If the weight ratio of the barrier resin to the inserted clay is greater than 99.0:1.0, the barrier improvement is negligible. 1320771 18784pif.doc The inserting clay is preferably organically inserted into the clay. The organic material to be inserted into the clay is preferably from 1 to 45% by weight. When the content of the organic material is less than 1% by weight, the 'inserted clay' has poor compatibility with the resin having barrier properties. When the content of the organic material is more than 45% by weight, it is difficult to insert a resin having a barrier property. The organic material has at least one functional group selected from the group consisting of primary ammonium to quaternary ammonium. , phosphonium, maleate, succinate, acrylate, benzylic hydrogen, oxazoline, and dimethyl Two hard fat waking money (dimethyldistearylammonium). The inserted clay comprises a material selected from the group consisting of montmorillonite, bentonite, kaolin, mica, saponite, laponite, saponite, beidellite, nontronite, strontite, worm to stone, kaolinite, and weikang. At least one material of earth, Shakang soil, Mage soil and Kenny soil; and the organic material preferably has a selected from the group consisting of first-grade ammonium to fourth-grade money, scales, cis-butanoic acid vinegar, broken vinegar vinegar, acrylic acid a functional group of benzyl gas, oxazoline and dimethyl distearyl ammonium. The ethylene-vinyl alcohol copolymer is included in the nano-composite, and the ethylene content in the ethylene-vinyl alcohol copolymer is preferably from 10 to 50 mol%. If the content of the & ene is less than 10 mol%, it is difficult to perform the glare molding because of poor workability. If the content of ethylene exceeds 50 mol%, oxygen and liquid resistance are insufficient. If the nanocomposite includes polyamine, the polyamine can be: 4.6, resistant to 6, resistant to 6.6, and only 6.10, accounting 7, and 8u', only to 9, 9 , nylon 12, nylon 46, MXD6, amorphous polyamine, 12 1320771 18784 pif.doc A copolymerized polyamine containing at least two of these polyamines or a mixture of at least two such polyamines. Amorphous polyamine refers to polyamine having insufficient crystallinity, that is, when measured by differential scanning calorimetry (DSC) (ASTM D-3417, 10 ° C/min), it does not have an endotherm. Crystal melting peak.

一般而言’可使用二胺與二叛酸來製傷聚醯胺。二胺 之實例包括:己二胺(hexamethylenediamine)、2-曱基戊 二胺(2-methylpentamethylenediamine)、2,2,4-三曱基己二 胺(2,2,4_trimethylhexamethylenediamine )、2,4,4_三甲基己 二胺(2,4,4-trimethylhexamethylenediamine)、雙(4-胺基環 己基)曱烧(bis(4-aminocyclohexyl)methane)、2,2-雙(4-胺 基環 己基) 亞異 丙基 (2,2-bis(4-aminocyclohexyl)isopropylidene )、1,4-二胺基環 己 烧 C 1,4-diaminocyclohexane )、 1,3- 二胺 基環己烷 ( 1,3-diaminocyclohexane )' 間二 L甲 苯 二 胺 C meta-xylenediamine ) 、1,5 •二 胺 基 戊 烧 ( 1,5-diaminopentane ) 、1,4- — 胺 基 丁 烷 ( 1,4-diaminobutane ) 、1,3- — 胺 基 丙 烧 ( 1,3-diaminopropane )、 2-乙 基· 二胺 基 丁 烧In general, diamines and ditoxaic acids can be used to make polyamines. Examples of diamines include: hexamethylenediamine, 2-methylpentamethylenediamine, 2,2,4-trimethylhexamethylenediamine, 2,4, 4_3,4-trimethylhexamethylenediamine, bis(4-aminocyclohexyl)methane, 2,2-bis(4-amino ring) Hexyl) 2,2-bis(4-aminocyclohexyl)isopropylidene, 1,4-diaminocyclohexene C 1,4-diaminocyclohexane ), 1,3-diaminocyclohexane ( 1 , 3-diaminocyclohexane ) 'meta-L-toluenediamine C meta-xylenediamine ), 1,5 • 1,5-diaminopentane, 1, 4-aminobutane (1,4-diaminobutane) ), 1,3-aminopropylpropane (1,3-diaminopropane), 2-ethyldiamine butylate

(2-ethyldiaminobutane ) ' 1,4-二胺基甲基環己炫 C 1,4-diaminomethylcyclohexane ) ' 甲院二甲苯二胺 (methane-xylenediamine)、烷基取代或未取代間苯二胺 (m-phenylenediamine )及對苯二胺(p-phenylenediamine ) 等。二缓酸之實例包括:烧基取代或未取代間苯二甲酸 13 1320771 I8784pif.doc (isophthalic acid)、對苯二甲酸(terephthalic acid)、己二 酉义(adipic acid )、癸二酸(sebacic acid )、丁二酸 (butanedicarboxylic acid)等。 使用脂知一胺與脂族二缓酸製備的聚酸胺為一般半晶 質聚醯胺(亦被稱為結晶耐綸),且不是非晶系聚醯胺。使 用芳族二胺與芳族二羧酸製備的聚醯胺難以使用一般的熔 融方法處理。 因而,當所使用的二胺及二羧酸之一為芳族且另一為 月g知時’較佳製備非晶系聚醯胺。非晶系聚酸胺的脂族基 較佳為CrCu脂族或CrCs脂族院基。非晶系聚醯胺的芳 族基較佳為經取代CrC6單環或雙環芳族基團。然而,在 本發明中上述非晶系聚醯胺都不是較佳的。舉例而言,當 在熱塑成形過程中加熱時或定向時,間二甲苯二胺己二酿 胺(metaxylenediamine adipamide)容易結晶,因此,其不 是較佳的。 較佳非晶系聚醯胺之實例包括:己二胺間苯二曱醯胺 (hexamethylenediamine isophthalamide);具有 99/1 至 60/40之間苯二甲酸/對苯二甲酸之比率的己二胺間苯二甲 醯胺/對苯二甲醯胺(terephthalamide)三元共聚物;2,2,4-三甲基 己二胺對苯二甲醯胺 (2,2,4-trimethylhexamethylenediamine terephthalamide) # 2,4,4-三甲基己二胺對苯二甲醯胺 (2,4,4-trimethylhexamethylenediamine terephthalamide )之 混合物;己二胺或2-甲基戊二胺與間苯二曱酸、對苯二甲 14 18784pif.doc 酸或其混合物之共聚物。當使用基於己二胺間苯二甲醯胺/ 對苯一甲醯胺之具有咼對苯二〒酸含量的聚醯胺時,其應 與諸如2-甲基二胺基戊烷(2-methyidiaminopentane)之另 一種一胺混合,以產生可加工的非晶系聚醯胺。 僅包含上述單體之上述非晶系聚醯胺可含有少量的諸 如己内醯胺(caprolactam)或月桂基内醯胺(lauryl lactam ) 之内醯胺作為共聚單體。重要的是該聚醯胺是非晶系的。 因此,可使用不使聚醯胺結晶的任何共聚單體。非晶系聚 醯胺中亦可包括約10重量。/。或更低諸如甘油(g〗ycer〇le)、 山 4 糖醇(sorbitol)、甲本石黃酿胺(toiuenesulfoneamide, Santicizer 8 monsanto )之液體或固體增塑劑。對於大多數 應用而言,非晶系聚醯胺的玻璃態轉換溫度Tg (於乾燥狀 恝下置測,意即水含量為〇12重量%或更低)為約7〇_17〇 C ’且較佳為約8〇-16〇。〇。未經摻合之非晶系聚醯胺在乾 燥狀態下具有大約125。(:之Tg。不清楚Tg的下限’但7〇 C為適當下限。也不清楚Tg的上限。然而,當使用具有 約170 C或更高之Tg的聚醯胺時’難以熱塑成形。因此, 由於Tg太高’不能熱塑成形具有具芳族基的酸及胺的聚 醯胺,且因此其不適宜於本發明之目的。 聚酿胺亦可為半晶質聚醯胺。通常使用諸如耐綸6或 耐論11之内酿胺或胺基酸來製備半晶質聚醯胺,或藉由縮 5諸如己一—胺與諸如琥站酸(succinic acid)、己二 酸或癸二酸之二元酸來製備。聚醯胺可為共聚物或三聚 物諸如己_胺/已二酸與乙酸内蕴胺(capr〇iactame)之 15 】8784pif.doc ^聚物(耐綸6, 66)。亦可使用兩個或兩個以上結晶聚醯 胺類之混合物。藉由此項技術中熟知之縮合聚合作用來製 備半晶質及非晶系聚醯胺。 若奈米複合物中包括離子聚合物,該離子聚合物較佳 =焊酸與乙烯之共聚物’具有每分鐘Q1至lG克之溶融 才曰數(190°C,2,160 克)。 奈〇=合物之含量較佳為〇·5 i 6〇重曼份,且更佳為 阻。右奈米複合物的含量小於0.5重量份,則 重、Γ、?良是可忽略的。若奈米複合物的含詈大於60 重置份’則難以加工。 一 地越===點土在具有阻絕性之樹脂中剝落 形成阻緯膜吧性越好。此是因為,剥落插入黏土 且最終缺機械性質, 質。因此,藉·由將且絕性及機械性 將奈米尺寸的插入黏:分二與插入黎土化合,且 插入黏土的接貞m本放树中,精此使聚合物鏈與 阻絕的能力最大化。’、、如大’來使形成對H體及液體之 有穩逆=,聚_的相容性 ,以形成具 性基團的烴聚二勿:極團的烴聚合物。當使用具有極 樹脂及對具有阻絕性之分增加相容劑對聚烯烴 有穩定結構的模製物品^、複5物的親和性,藉此獲得具 16 】8784pif.doc 相容劑可包括選自下列各物之一種化合物:環氧改質 聚苯乙嫜共聚物(epoxy-modified polystyrene copolymer)、 乙烯-乙烯酐-丙烯酸共聚物、乙烯-丙烯酸乙酯共聚物、乙 烯-丙烯酸烷基酯-丙烯酸共聚物、順丁烯二酸酐改質(接 枝)高密度聚乙烯、順丁烯二酸酐改質(接枝)聚丙烯、 順丁烯二酸酐改質(接枝)直鏈低密度聚乙烯、乙烯-(甲 基)丙烯酸烷基酯-(曱基)丙烯酸共聚物、乙烯-丙烯酸 丁酯共聚物、乙烯-乙酸乙烯酯共聚物、順丁烯二酸酐改質 (接枝)乙烯-乙酸乙烯酯共聚物及其改質體。 相容劑含量較佳為1至30重量份,且更佳為3至ι5 重量份。若相容劑含量小於1重量份,則由組合物模製之 物品的機械性質差。若相容劑含量大於30重量份,則組合 物難以成形。 當使用環氧改質聚苯乙烯共聚物作為相容劑時,較隹 為含有包含70至99重量份之苯乙烯及1至30重量份之式 1所代表的環氧化合物之主鏈及包含1至8〇重量份之式2 所代表的丙烯酸單體之支鏈的共聚物。 Η Η ~"R~C\7C—R' ( 1 ) 其中R與R各獨立為Ci-C2〇脂族殘基或末端具有錐 鍵的C5-C20芳族殘基。 又 (2) (2)1320771 18784pif.doc 順丁烯二酸酐改質(接枝)高密度聚乙烯、順丁烯二 酸酐改質(接枝)聚丙烯、順丁烯二酸酐改質(接枝)直 鏈低密度聚乙烯及順丁烯二酸酐改質(接枝)乙烯-乙酸乙 烯酯共聚物各較佳包含以主鏈之100重量份計具有0.1至 10重量份之順丁烯二酸酐的支鏈。當順丁烯二酸酐含量小 於0.1重量份時,其不起相容劑作用。當順丁烯二酸酐含 量大於10重量份時,由於令人討厭的氣味,其不是較佳的。 藉由於顆粒混合器中以恆定組成比干摻合具有阻絕性 之顆粒狀奈米複合物、相容劑及聚烯烴樹脂來製備本發明 之組合物。 藉由模製經乾混合之組合物及用氟塗覆模製容器之一 内壁來獲得根據本發明的具有高阻絕性的物品。 意即,該方法包括:藉由乾混合40至96重量份的聚 烯烴樹脂、0.5至60重量份的具有阻絕性之奈米複合物及 1至3 0重量份的相容劑來製備具有阻絕性之奈米複合物組 合物,該奈求複合物包括一插入黏土及至少一種選自由下 列各物組成之群之具有阻絕性的樹脂:乙烯-乙烯醇 (EVOH )共聚物、聚醯胺、離子聚合物及聚乙烯醇 (PVA);模製該組合物形成一物品;及用氟塗覆該模製物 品之一内壁。 自乾混合奈米複合物組合物,藉由在擠壓機中熔融摻 合該組合物並模製熔融摻合物,並接著用氟塗覆模製物品 18 18784ρΐ£^0ς 之-内壁來製造具有高阻絕性的物品。可經由吹塑成形、 鞭塵成形、加堡成形或射出成形來製造該物品。 具有高阻絕性之物品可為容器、薄月、膜或管。 了使用鬲/皿σ人塑成形法(Koyutakahukikomi成形法) 執行氟塗覆,且氟塗層之厚度可為〇 〇2至11//m。在 ,壁接觸奈米複合物组合物(容器主要由其組成}前,^ ^塗覆壁防止内含物穿透。即使當内含物穿透氟塗覆^ 時,由奈米複合物組合物組成的外壁防止内含物穿透,$ 此展示出優良的阻絕性。 9 、以下,經由實例更詳細地描述本發明。下列實例僅欲 增加對本發明的理解,且不欲限定本發明之範疇。 實例 以下實例中所使用的材料如下: EVOH · E105B (Kuraray 5 Japan) 耐論 6 : ΕΝ 500 (KP Chemicals) 離子聚合物:SURLYN 8527 (Dupont,U.S.A.) HDPE_g-MAH:相容劑,ΡΒ3009 (CRAMPTON) 聚烯烴樹脂:高密度聚乙烯(BDO 390,LG ClffiM, ^融指數:每10分鐘0.3克,密度:0.949克/立方公分 (g/cm3)) 黏土: Closite 30B (SCP) 熱穩定劑:IR 1098 (Songwonlnc.) 製備實例1 (EVOH/插入黏土奈米複合物的製備) 19 1320771 18784pif.doc 將97重量。/〇的乙烯_乙烯醇共聚物(Ev〇h;E-105B (乙浠含I . 44莫耳%) ; Kuraray ; Japan ;炫融指數:每 . 10分鐘5.5克;密度:1.14克/立方公分)放入雙螺桿擠壓 機(SMPlatek同向雙螺桿擠壓機;炉40)之主料斗中。接 著’分別將3重量%之作為插入黏土的有機蒙脫土 (Southern Intercalated Clay Products,USA ; C20A)以及 以EVOH共聚物與有機蒙脫土之總1〇〇重量份計之〇.i重 量份的作為熱穩定劑的IR 1〇98放入雙螺桿擠壓機之側給 ® 料斗中來製備顆粒狀EVOH/插入黏土奈米複合物。擠壓溫 度條件為 180-190-200-200-200-200-2001,螺桿以 300 轉/ 分鐘(ipm)旋轉,且排出條件為4〇千克/小時(kg/hr)。 - 製備實例2 (耐綸6/插入黏土奈米複合物的製備) 將97里夏%的聚酿胺(耐綸6)放入雙螺桿擠壓機(sm Platek同向雙螺桿擠壓機;φ4〇)之主料斗中。接著,分 別將3,量%之作為插入黏土的有機蒙脫土以及以&醯二 籲 與有機冡脫土之總10〇重量份計之〇.1重量份的作為熱穩 定劑的m 1098放入雙螺桿擠壓機之側給料斗中來製備顆 - 粒狀的聚醯胺/插入黏土奈米複合物。擠壓溫度條件為 220-225-245-245-245-245-245。(:,螺桿卩 3〇0 轉/分鏠方, , 轉,且排出條件為40千克/小時。 疋 製備實例3 (離子聚合物/插入黏土奈米複合物的製備)(2-ethyldiaminobutane ) ' 1,4-diaminomethylcyclohexyl C 1,4-diaminomethylcyclohexane ) ' methane-xylenediamine, alkyl substituted or unsubstituted m-phenylenediamine (m -phenylenediamine) and p-phenylenediamine. Examples of di-lowering acid include: pyridyl substituted or unsubstituted isophthalic acid 13 1320771 I8784 pif.doc (isophthalic acid), terephthalic acid, adipic acid, sebacic acid (sebacic) Acid ), butanedicarboxylic acid, and the like. The polyamine prepared using the lipid monoamine and the aliphatic bis-acid is a general semicrystalline polyamine (also referred to as crystalline nylon) and is not an amorphous polyamine. Polyamines prepared using aromatic diamines and aromatic dicarboxylic acids are difficult to handle using conventional melting methods. Thus, when one of the diamines and dicarboxylic acids used is aromatic and the other is a month, it is preferred to prepare an amorphous polyamine. The aliphatic group of the amorphous polyamine is preferably a CrCu aliphatic or a CrCs aliphatic group. The aromatic group of the amorphous polyamine is preferably a substituted CrC6 monocyclic or bicyclic aromatic group. However, the above amorphous polyamines are not preferred in the present invention. For example, metaxylenediamine adipamide is easily crystallized when heated or oriented during the thermoforming process, and therefore, it is not preferred. Examples of preferred amorphous polyamines include: hexamethylenediamine isophthalamide; hexamethylenediamine having a ratio of phthalic acid/terephthalic acid between 99/1 and 60/40 Terephthalamide terpolymer: 2,2,4-trimethylhexamethylenediamine terephthalamide #2,4-trimethylhexamethylenediamine terephthalamide # a mixture of 2,4,4-trimethylhexamethylenediamine terephthalamide; hexamethylenediamine or 2-methylpentanediamine and isophthalic acid, a copolymer of phthalic acid 14 18784pif.doc acid or a mixture thereof. When a polydecylamine having a terpene terephthalic acid content based on hexamethylenediamine m-xylyleneamine/p-benzoic acidamine is used, it should be combined with, for example, 2-methyldiaminopentane (2- Another monoamine of methyidiaminopentane) is mixed to produce a processable amorphous polyamine. The above amorphous polyamine containing only the above monomers may contain a small amount of a decylamine such as caprolactam or lauryl lactam as a comonomer. It is important that the polyamine is amorphous. Thus, any comonomer that does not crystallize the polyamine can be used. Approximately 10 weights may also be included in the amorphous polyamine. /. Or lower liquid or solid plasticizers such as glycerol (g ycer〇le), sorbitol, toiuenesulfoneamide (Santicizer 8 monsanto). For most applications, the glass transition temperature Tg of amorphous polyamine (measured under dry conditions, meaning that the water content is 〇12% by weight or less) is about 7〇_17〇C ' And preferably about 8〇-16〇. Hey. The unblended amorphous polyamine has about 125 in a dry state. (Tg of Tg. The lower limit of Tg is not known 'but 7 〇 C is a suitable lower limit. The upper limit of Tg is also unclear. However, when polyamine having a Tg of about 170 C or higher is used, it is difficult to thermoform. Therefore, since Tg is too high, it is not possible to thermoform a polyamine having an aromatic group-containing acid and an amine, and thus it is not suitable for the purpose of the present invention. The polystyrene may also be a semi-crystalline polyamine. Preparation of semi-crystalline polyamines using an internal amine or amino acid such as nylon 6 or resistant to 11 or by condensing 5 such as hexyl-amine with succinic acid, adipic acid or It can be prepared by the dibasic acid of sebacic acid. The polydecylamine can be a copolymer or a terpolymer such as hexamethylene/adipic acid and caprylic acid amine (capr〇iactame) 15]8784pif.doc ^polymer (resistant Polyamide 6, 66). Mixtures of two or more crystalline polyamidoamines may also be used. Semi-crystalline and amorphous polyamines are prepared by condensation polymerization well known in the art. Included in the ionic polymer, the ionic polymer preferably = copolymer of solder acid and ethylene 'has a melting rate of Q1 to 1G per minute. The number (190 ° C, 2,160 g). The content of the naphthalene = compound is preferably 〇 · 5 i 6 〇 heavy parts, and more preferably resistance. The content of the right nano composite is less than 0.5 parts by weight, The weight, yttrium, and yttrium are negligible. If the yttrium of the nanocomposite is greater than 60, the replacement part is difficult to process. The more the land === the point soil is peeled off in the resin with barrier properties to form a damper film. The better, this is because the exfoliation is inserted into the clay and ultimately lacks mechanical properties. Therefore, it is necessary to insert and bond the nano-sized inserts into the clay and insert them into the clay. The 贞m is placed in the tree, which maximizes the ability of the polymer chain and the resistance to block. ',, such as large' to form a stable anti-H body and liquid =, poly_ compatibility, to form A hydrocarbon group of a polar group: a hydrocarbon polymer of a polar group. When using a resin having a polar resin and a barrier property, the compatibilizing agent has a stable structure to the polyolefin, and the affinity of the molded article To obtain a 16]8784pif.doc compatibilizer may comprise a compound selected from the group consisting of: epoxy modified poly Epoxy-modified polystyrene copolymer, ethylene-vinyl anhydride-acrylic acid copolymer, ethylene-ethyl acrylate copolymer, ethylene-alkyl acrylate-acrylic acid copolymer, maleic anhydride modification (grafting High-density polyethylene, maleic anhydride modified (grafted) polypropylene, maleic anhydride modified (grafted) linear low-density polyethylene, ethylene-alkyl (meth)acrylate-( Mercapto)acrylic acid copolymer, ethylene-butyl acrylate copolymer, ethylene-vinyl acetate copolymer, maleic anhydride modified (grafted) ethylene-vinyl acetate copolymer and modified body thereof. The content of the compatibilizer is preferably from 1 to 30 parts by weight, and more preferably from 3 to 5% by weight. If the compatibilizer content is less than 1 part by weight, the article molded from the composition is inferior in mechanical properties. If the compatibilizer content is more than 30 parts by weight, the composition is difficult to form. When an epoxy modified polystyrene copolymer is used as a compatibilizing agent, it is preferably a main chain comprising 70 to 99 parts by weight of styrene and 1 to 30 parts by weight of the epoxy compound represented by Formula 1 and comprising 1 to 8 parts by weight of a branched copolymer of an acrylic monomer represented by Formula 2. Η Η ~"R~C\7C-R' (1) wherein R and R are each independently a Ci-C2 steroid residue or a C5-C20 aromatic residue having a tapered bond at the end. (2) (2) 1320771 18784pif.doc Maleic anhydride modified (grafted) high density polyethylene, maleic anhydride modified (grafted) polypropylene, maleic anhydride modified (connected The branched low-density polyethylene and the maleic anhydride modified (grafted) ethylene-vinyl acetate copolymer each preferably have 0.1 to 10 parts by weight of maleicene based on 100 parts by weight of the main chain. Branching of an acid anhydride. When the maleic anhydride content is less than 0.1 part by weight, it does not function as a compatibilizer. When the maleic anhydride content is more than 10 parts by weight, it is not preferred due to an unpleasant odor. The composition of the present invention is prepared by dry blending a barrier-like granular nanocomposite, a compatibilizing agent, and a polyolefin resin in a pellet mixer at a constant composition ratio. The article having high resistance according to the present invention is obtained by molding the dry-mixed composition and coating the inner wall of one of the containers with fluorine. That is, the method comprises: forming a barrier by dry mixing 40 to 96 parts by weight of a polyolefin resin, 0.5 to 60 parts by weight of a barrier-resistant nanocomposite, and 1 to 30 parts by weight of a compatibilizing agent. a nanocomposite composition comprising a plugged clay and at least one resin selected from the group consisting of ethylene-vinyl alcohol (EVOH) copolymer, polyamine, An ionic polymer and polyvinyl alcohol (PVA); molding the composition to form an article; and coating the inner wall of one of the molded articles with fluorine. The self-drying hybrid nanocomposite composition is manufactured by melt blending the composition in an extruder and molding the molten blend, and then coating the inner wall of the article 18 18784 ΐ ^ ^ 用 with fluorine Items with high resistance. The article can be made by blow molding, whip dust forming, Kayborg forming or injection molding. Articles with high resistance can be containers, thin months, membranes or tubes. Fluorine coating is carried out using a σ/ dish σ human plastic forming method (Koyutakahukikomi forming method), and the thickness of the fluorine coating layer may be 〇2 to 11 //m. Before the wall contacts the nanocomposite composition (the container is mainly composed of it), the coating wall prevents the inclusions from penetrating. Even when the contents penetrate the fluorine coating, the nanocomposite composition The outer wall of the composition prevents penetration of the inclusions, which demonstrates excellent resistance. 9. The following is a more detailed description of the invention by way of example only. The following examples are merely intended to increase the understanding of the invention and are not intended to limit the scope of the invention EXAMPLES The materials used in the following examples are as follows: EVOH · E105B (Kuraray 5 Japan) 耐 6 6 : ΕΝ 500 (KP Chemicals) Ionic polymer: SURLYN 8527 (Dupont, USA) HDPE_g-MAH: Compatibilizer, ΡΒ3009 ( CRAMPTON) Polyolefin Resin: High Density Polyethylene (BDO 390, LG ClffiM, Melt Index: 0.3 g per 10 minutes, Density: 0.949 g/cm3 (g/cm3)) Clay: Closite 30B (SCP) Heat Stabilizer :IR 1098 (Songwonlnc.) Preparation Example 1 (Preparation of EVOH/inserted clay nanocomposite) 19 1320771 18784 pif.doc 97 wt./〇 ethylene-vinyl alcohol copolymer (Ev〇h; E-105B (B)浠 contains I. 44% by mole); Kuraray; Japan; Index: 5.5 g per 10 minutes; density: 1.14 g/cm 3 ) placed in the main hopper of a twin-screw extruder (SMPlatek co-rotating twin-screw extruder; furnace 40). Then '3 wt% respectively As an organic montmorillonite inserted into clay (Southern Intercalated Clay Products, USA; C20A) and 〇.i parts by weight of the total weight of the EVOH copolymer and the organic montmorillonite, IR 1 as a heat stabilizer 〇98 was placed in the side of the twin-screw extruder into the hopper to prepare a granular EVOH/insert clay nanocomposite. The extrusion temperature conditions were 180-190-200-200-200-200-2001 and the screw was 300. Rotation / minute (ipm) rotation, and the discharge condition is 4 〇 kg / hr (kg / hr) - Preparation Example 2 (Preparation of nylon 6 / insert clay nanocomposite) 97% of the polyamine (Nylon 6) placed in the main hopper of a twin-screw extruder (sm Platek co-rotating twin-screw extruder; φ4〇). Next, 3, % of the organic montmorillonite inserted into the clay and & 醯 吁 与 与 与 与 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡 冡098 was placed in the side feed hopper of a twin-screw extruder to prepare a granulated polyamide/inserted clay nanocomposite. The extrusion temperature conditions are 220-225-245-245-245-245-245. (:, screw 卩 3〇0 rpm / 鏠, , and the discharge condition is 40 kg / hr. 制备 Preparation Example 3 (Preparation of ionic polymer/inserted clay nanocomposite)

將97重量°/◦的離子聚合物放入雙螺桿擠壓機(SM 20 18784pif.docPut 97 weight ° / ◦ ionic polymer into a twin screw extruder (SM 20 18784pif.doc

Platek同向雙螺桿擠壓機;炉40)之主料斗中。接著,分 別將3重量%之作為插入黏土的有機蒙脫土以及以離子聚 合物與有機蒙脫土之總100重量份計之〇·丨重量份的作為 熱穩定劑的IR 1098放入雙螺桿擠壓機之側給料斗中來製 備顆粒狀的離子聚合物/插入黏土奈米複合物。擠壓溫度條 件為 220-225-245-245-245-245-245。(:,螺桿以 300 轉/分鐘 旋轉’且排出條件為40千克/小時。 實例1 於雙錐型混合器(dumble mixer )中乾混合25重量份 之製備實例1獲得的EVOH/插入黏土奈米複合物、ό重量 份之相容劑以及69重量份之高密度聚乙烯,且使用吹塑成 开(SMC 吹塑成形機,6〇phi)於 19〇-205-205-205。〇之 擠壓溫度條件下_乾混合物。將自吹錢形機末端擦出 的,坯放^定形為1000毫升農用化學品容器之模中。用惰 t生,體(氮).對型链加壓6秒至】碎/平方英叶(Μ堵) 二[力。接著’降低容器中的壓力且使容魏氣Μ秒。 用3有氮氣及!至1〇%之說氣的反應性氣體對容器 =6秒至約100碎/平方英忖(〇 7兆帕(卿〇之壓 斤。”後,釋放壓力且使容器脫氣15秒。接著,用惰性 加壓6秒至約!㈣/平方英吁(〇 7兆帕) 惰iC ’釋_力且使容器脫氣h5秒。最後,用 帕)容J再加屢6秒至約1〇"/平才英# (〇.7兆 “器:Πί=ί狀態且自模中 有0.2//m尽的氟塗層的内 1320771 18784pif.doc 壁。 實例2 於雙錐型混合器(mydcm-ioo,MYE0NG wo〇 micron SYSTEM)中將25重量份之製備實例2中獲得 的=綸6/插入黏土奈来複合物、6重量份之相容劑以及69 ^之问密度聚乙烯乾混合3G分鐘。使財塑成形機 (SMC吹塑成形機,6〇phi)於隱2〇5_2〇5_2〇5〇c之播厚 溫度條件下播壓乾混合物。將自吹塑成形機末端播出^型 3放广定形為誦毫升農聽學品容器之射。用惰性氣 體(氮)對型坯加壓6秒至1〇〇磅/平方英吋之壓力。接著, ,低容器中的壓力且使容器脫氣15秒。隨後,用含有氮 矾及1至10%之氟氣的反應性氣對容器再加壓6秒至約 1 二0^,/平方英吋(〇7兆帕)之壓力。其後,釋放壓力且 使各益脫氣1.5秒。接著’用惰性氮氣對容器再加壓6秒 至約10^磅/平方英吋(0 7兆帕)之壓力。其後,釋放屢 力且使容器脫氣1.5秒。最後,用惰性氮氣對容器再加壓 至約100磅/平方英吋(0 7兆帕)之壓力。其後,使 谷°。回復至大氣壓力狀態且自模中移除。所得模製容器含 有一具有0.2/zm厚的氟塗層的内壁。 實例3 於雙錐型混合器(MYDCM-100, MYEONG W0〇 MICRON SYSTEM)中將4重量份之製備實例2中獲得的 =綸6/插入黏土奈米複合物、2重量份之相容劑以及94重 量份之高密度$乙婦乾混合30 >鐘。使用吹塑成形機 22 1320771 18784pif.doc (SMC 吹塑成形機,60phi)於 190-205-205-205。(:之擠壓 溫度條件下擠壓乾混合物。將自吹塑成形機末端擠出的型 •, 坯放入定形為⑻毫升農用化學品容器之模中。用惰性氣 * . 體(氮)對型坯加壓6秒至100磅/平方英吋之壓力。接著, 降低容器中的壓力且使容器脫氣M秒。隨後,用含有氮 氣及1至10%之氟氣的反應性氣體對容器再加壓6秒至約 1〇〇磅/平方英吋(0.7兆帕)之壓力。其後,釋放壓力且 使容器脫氣丨.5秒。接著,用惰性氮氣對容器再加壓ό秒 攀觸_辦方射(0.7兆帕)之屋力。其後,釋放塵 力且使容器脫氣1.5秒。最後,用惰性氮氣對容器再加壓 6秒至1〇〇磅/平方英吋(〇·7兆帕)之壓力。其後,使^ 3 口仅至大氣壓力狀恶且自模中移除。所得模製容器么有 一具有0.2//m厚的氟塗層的内壁。 實例4 於雙錐型混合器(MYDCM-100, MYEONG WOO MICRON SYSTEM)中將40重量份之製備實例2中獲得 • 的耐綸6/插入黏土奈米複合物、Μ重量份之相容劑以及 42重量份之高密度聚乙烯乾混合3〇分鐘。使用吹塑成形 機(SMC 吹塑成形機,60phi)於 190_2〇5_2〇5_2〇5t:之擠 壓溫度條件下擠壓乾混合物。將自吹塑成形機末端擠出的 型坯放入定形為1000亳升農用化學品容器之模中。用惰性 氣體(氮)對型坯加壓6秒至100磅/平方英吋之壓力。接 著,降低容器中的壓力且使容器脫氣15秒。隨後,用含 有氮氣及1至10%之氟氣的反應性氣體對容器再加壓6秒 23 1320771 18784pif.doc 至約100磅/平方英吋(0.7兆帕)之壓力。其後,釋放壓 力且使容器脫氣1.5秒。接著,用惰性氮氣對容器再加壓 . 6秒至約100磅/平方英吋(〇.7兆帕)之壓力。其後,释 ._ 放壓力且使容器脫氣1.5秒。最後,用.惰性氮氣對容器再 加廢6秒至約100碎/平方英叶(0.7兆帕)之屢力。其後, 使容器回復至大氣壓力狀態且自模中移除。所得模製容器 含有一具有0·2/ζπι厚的氟塗層的内壁。 實例5 鲁 於雙錐型混合器(MYDCM-100,MYEONG W〇〇 MICRON SYSTEM)中將25重量份之製備實例3中獲得 • 的離子聚合物/插入黏土奈米複合物、6重量份之相容劑以 - 及69重量份之高密度聚乙烯乾混合30分鐘。使用吹塑成 形機(SMC吹塑成形機,60phi)於190-205-205-205。〇之 擠壓溫度條件下撥麼乾混合物。將自吹塑成形機末端擠出 的型坯放入定形為1000毫升農用化學品容器之模中。用惰 性氣體(氮)對型坯加壓6秒至100磅/平方英吁之壓力。 • 接著,降低容器中的壓力且使容器脫氣1.5秒。隨後,用 含有氮氣及1至10%之氟氣的反應性氣體對容哭 .秒至約餅方英忖⑽兆帕)之壓力#放6 壓力且使容态脫氣1.5秒。接著,用惰性氮氣對容器 • 壓6秒至約1〇〇磅/平方英吋(〇·7兆帕)之屄力二口 釋放壓力且使容器脫氣l5秒。最後,用惰 再加壓6秒至約100碎/平方英叶(〇.7兆帕) 後,使容器回復至大氣屢力狀態且自模中移 24 1320771 18784pif.doc 容器含有一具有0.2#m厚的氟塗層的内壁。 實例6 於190-205-205-205Ϊ之擠壓溫度條件下’以乾混合狀 態,分別通過帶式給料器K-TR〇N第】、2及3號將15重 里伤之製備實例2中獲得的耐綸6/插入黏土奈米複合物、 7重里份之相容劑以及78重量份之高密度聚乙烯同時放入 吹塑成形機(SMC吹塑成形機,6〇 phi)之主料斗中。將 自吹塑成形機末端㈣的型述放入定形為_ 化學品容器之模中。用惰性氣體(氮)對型链加壓6秒至 =^^ 之勤。接著,降低容財㈣力且使容 應=二有氮氣及1至之氟氣的反 用,产脖:ί Ά ’釋放屢力且使容器脱氣1.5秒。接著, 用惰性虱氣對宏哭i v便a 兆怡)之愿力^ 秒至約100石旁/平方英时(〇.7 後,用惰性氮氣對玄哭益,,使谷减乳秒。最 ⑽兆帕)之展秒至'約1〇0石旁/平方英吋 且自模令移除。$ 吏容器回復至大氣麼力狀態 塗層的内壁i、于旲、谷盗含有一具有厚的氟 比較實例1 1相同之方黏土之外’以與實例 比較實例2 a之谷裔。 除了不使用有機蒙稅土作為插入黏土之外’以與實例 25 1320771 18784pif.doc 2相同之方式製造具有阻絕性之容器。 比較實例3 时 於]85-195-195_195t之雜溫度條件τ,使用吹塑成 形SMC。人塑成形機’ 6〇phi)擠壓聚乙烯(BD的叩, 古]將自口人塑成开>機末端播出的型链放人定开)為觸〇 笔升農用化學品容器之模中。用,隋性氣體(氮)對型这加 壓6秒至100辦方英对之壓力。接著,降低容器中的麼 使谷器脫氣h5秒。隨後,用含有氮氣及1至10%之 氟氣的反應性軋體對容器再加壓6秒至約丨⑼碎/平方英忖 (^7兆帕)之愿力。其後,釋放麼力且使容器脫氣秒。 接4用Μ性氮氣對容器再加壓6秒至約】⑽碎/平方英吋 ^ 〇·7兆帕)之㈣。其後,釋放屢力且使容器脫氣i 5秒。 取後,周惰性氮氣對容器再加壓6秒至約1〇〇磅/平方英吋 (0.7—兆帕)之麼力。其後,使容器回復至大氣屢力狀態 且自模中移除。所得模製容器含有一具有〇2_厚的氟 塗層的内壁。 實驗性實例 a)液體阻絕性 將甲苯、Desys除草劑(! %之溴氰菊酯(ddtametrine ) +乳化劑、穩定劑及溶劑;KyungNong)、Bats^昆蟲劑 (50/。之BpMC + 5〇%2乳化劑及溶劑)及水放入實例1 至6及比較實例丨至3中所製造的容器中。接著,3〇天後, 於50°C強制排出條件下測定重量變化。對於甲苯而言,進 一步於室溫下測定重量變化。 26 1320771 18784pif.doc b )氣體阻絕性(立方公分/平方米·天·大氣壓力 (cc/m2. day · atm)) 於23°C之溫度及50%相對濕度下,將實例1至6以及 比較實例1至3中所製備的容器單獨放置1天。接著,測 定氣體穿透率(MoconOX-TRAN 2/20,U.S.A)。Platek co-rotating twin-screw extruder; the main hopper of furnace 40). Next, 3 wt% of the organic montmorillonite as the clay and the IR 1098 as the heat stabilizer in terms of 100 parts by weight of the total weight of the ionic polymer and the organic montmorillonite were placed in the twin screw. The side of the extruder is fed into a hopper to prepare a granular ionic polymer/inserted clay nanocomposite. The extrusion temperature conditions are 220-225-245-245-245-245-245. (:, the screw was rotated at 300 rpm) and the discharge condition was 40 kg/hr. Example 1 25 parts by weight of EVOH/inserted clay obtained in Preparation Example 1 was dry-mixed in a dumble mixer (dumble mixer) The composite, the bismuth by weight of the compatibilizer and 69 parts by weight of the high-density polyethylene, and using blow molding to open (SMC blow molding machine, 6 phi) at 19 〇 - 205-205-205. Under the condition of pressure temperature, the dry mixture will be wiped out from the end of the blown machine, and the blank will be shaped into a mold of 1000 ml of agrochemical container. Use inertia, body (nitrogen). Pressurize the type chain 6 Seconds to 】 broken / square English leaves (blocking) two [force. Then 'reduced the pressure in the container and let the Wei Wei gas second. Use 3 with nitrogen and! to 1%% of the gas reactive gas to the container =6 seconds to about 100 cc/sq ft (〇7 MPa (clear 。.), release the pressure and degas the container for 15 seconds. Then, pressurize with inert gas for 6 seconds to about! (four) / square Ying Yu (〇7 MPa) Idle iC 'release _ force and degas the container for h5 seconds. Finally, use Pa) Rong J and add 6 seconds to about 1 〇"/平才英# (〇.7 "Device: Πί=ί state and there is a fluorine coating of inner 1220771 18784pif.doc wall with 0.2//m in the mold. Example 2 will be in a double cone mixer (mydcm-ioo, MYE0NG wo〇micron SYSTEM) 25 parts by weight of the yoke 6/insert clay nitrite compound obtained in Preparation Example 2, 6 parts by weight of the compatibilizer, and 69 Å of the density polyethylene were dry-mixed for 3 G minutes to make a plastic molding machine (SMC blow molding) The forming machine, 6〇phi), is used to dry the mixture under the condition of the thickness of the hidden 2〇5_2〇5_2〇5〇c. The end of the self-blow molding machine is broadcasted into a shape of 3 ml. Injection of the product container. The parison is pressurized with an inert gas (nitrogen) for a pressure of from 6 seconds to 1 Torr/square Torr. Then, the pressure in the vessel is lowered and the vessel is degassed for 15 seconds. The reaction gas of nitrogen bismuth and 1 to 10% of fluorine gas repressurizes the container for 6 seconds to a pressure of about 1 0.02 Å/〇 吋 (〇7 MPa). Thereafter, the pressure is released and the benefits are obtained. Degas for 1.5 seconds. Then re-pressurize the vessel with inert nitrogen for 6 seconds to a pressure of about 10 ^ psi (0 7 MPa). Thereafter, release the force and remove the container. 1.5 seconds. Finally, the vessel was repressurized with inert nitrogen to a pressure of about 100 psi (0 7 MPa). Thereafter, the valley was returned to atmospheric pressure and removed from the mold. The molded container contained an inner wall having a fluorine coating layer of 0.2/zm thick. Example 3 4 parts by weight of the obtained yoke obtained in Preparation Example 2 in a double cone type mixer (MYDCM-100, MYEONG W0〇MICRON SYSTEM) 6/Into the clay nanocomposite, 2 parts by weight of the compatibilizer, and 94 parts by weight of the high density $48 dry mix 30 > A blow molding machine 22 1320771 18784 pif.doc (SMC blow molding machine, 60 phi) was used at 190-205-205-205. (: Extrusion of the dry mixture under extrusion temperature conditions. The type extruded from the end of the blow molding machine, and the blank into a mold of a (8) ml agrochemical container. Use inert gas*. Body (nitrogen) The parison is pressurized for a pressure of from 6 seconds to 100 pounds per square inch. Next, the pressure in the vessel is lowered and the vessel is degassed for M seconds. Subsequently, a reactive gas pair containing nitrogen and 1 to 10% of fluorine gas is used. The container is then pressurized for a further 6 seconds to a pressure of about 1 〇〇 psi (0.7 MPa). Thereafter, the pressure is released and the vessel is degassed for 5 seconds. Next, the vessel is repressurized with inert nitrogen. Seconds climbs to the house (0.7 MPa). After that, the dust is released and the container is degassed for 1.5 seconds. Finally, the container is repressurized with inert nitrogen for 6 seconds to 1 lb./sq. The pressure of 吋 (〇·7 MPa) was followed, and the port was only removed to atmospheric pressure and removed from the mold. The resulting molded container had an inner wall having a fluorine coating of 0.2//m thick. Example 4 40 parts by weight of the nylon 6/insert obtained in Preparation Example 2 in a double-cone mixer (MYDCM-100, MYEONG WOO MICRON SYSTEM) The nanocomposite, the bismuth by weight compatibilizer and 42 parts by weight of high density polyethylene were dry mixed for 3 minutes. Using a blow molding machine (SMC blow molding machine, 60 phi) at 190_2 〇 5_2 〇 5 2 〇 5t: The dry mixture was extruded at the extrusion temperature. The parison extruded from the end of the blow molding machine was placed in a mold set to a 1000 liter agrochemical container. The parison was pressurized with an inert gas (nitrogen). Pressure in seconds to 100 psi. Then, reduce the pressure in the vessel and degas the vessel for 15 seconds. Then, pressurize the vessel for 6 seconds with a reactive gas containing nitrogen and 1 to 10% fluorine. 23 1320771 18784pif.doc to a pressure of about 100 psi (0.7 MPa). Thereafter, the pressure is released and the vessel is degassed for 1.5 seconds. Then, the vessel is repressurized with inert nitrogen. 6 seconds to about 100 Pounds per square inch (〇.7 MPa). Thereafter, release the pressure and degas the vessel for 1.5 seconds. Finally, add the waste to the vessel for 6 seconds to about 100 cc/square with inert nitrogen. The British leaf (0.7 MPa) is repeated. After that, the container is returned to atmospheric pressure and removed from the mold. The obtained molded container contained an inner wall having a fluorine coating layer having a thickness of 0·2/ζπι. Example 5 25 parts by weight of Preparation Example 3 in a double cone type mixer (MYDCM-100, MYEONG W〇〇MICRON SYSTEM) The ionic polymer/inserted clay nanocomposite obtained, the 6 parts by weight of the compatibilizer, and the 69 parts by weight of the high density polyethylene were dry-blended for 30 minutes. Using a blow molding machine (SMC blow molding machine, 60 phi) at 190-205-205-205.拨 The dry mixture is squeezed under the conditions of extrusion temperature. The parison extruded from the end of the blow molding machine was placed in a mold set to a 1000 ml agrochemical container. The parison is pressurized with an inert gas (nitrogen) for a pressure of 6 seconds to 100 psi. • Next, reduce the pressure in the container and degas the container for 1.5 seconds. Subsequently, a reactive gas containing nitrogen and 1 to 10% of fluorine gas was used to cough. The pressure of seconds to about 10 MPa (10 MPa) was placed at 6 pressures and the contents were degassed for 1.5 seconds. Next, pressurize the vessel with inert nitrogen for 6 seconds to about 1 lb./sq. ft. (7 MPa) and release the vessel for 15 seconds. Finally, after repressurizing with inert gas for 6 seconds to about 100 cc/square y (〇.7 MPa), the container is returned to the atmosphere and moved from the mold. 24 1320771 18784pif.doc The container contains one with 0.2# The inner wall of the m-thick fluorine coating. Example 6 was obtained in the preparation example 2 of the 190-205-205-205 挤压 extrusion temperature condition in the dry mixed state, respectively, by the belt feeder K-TR〇N No. 2, No. 3 and the 15 heavy wounds. Nylon 6/insert clay nanocomposite, 7-fold compatible compatibilizer and 78 parts by weight of high-density polyethylene are simultaneously placed in the main hopper of a blow molding machine (SMC blow molding machine, 6〇phi) . The pattern from the end (4) of the blow molding machine is placed in a mold that is shaped as a chemical container. Pressurize the chain with an inert gas (nitrogen) for 6 seconds to =^^. Next, reduce the fortune (4) force and make the capacity = two with nitrogen and 1 to the fluorine gas, the neck: ί Ά ‘ release the force and degas the container for 1.5 seconds. Then, with the inert gas, the macro will cry iv will be a singular force ^ seconds to about 100 stone side / square inch time (〇.7, with inert nitrogen on the Xuan Cry, to make the valley reduce milk seconds. The most (10) megapascals of the exhibition seconds to 'about 1 〇 0 stone side / square inch and removed from the mold. $ 吏 回复 回复 回复 回复 回复A container having a barrier property was produced in the same manner as in Example 25 1320771 18784 pif.doc 2 except that organic Mongolian soil was not used as the inserting clay. In Comparative Example 3, a mixed temperature condition τ of 85-195-195_195t was used, and blow molding was used to form SMC. Plastic molding machine '6〇phi) extruded polyethylene (BD 叩, ancient) will be molded from the mouth of the mouth > the end of the machine broadcasted the type of chain released to open) for the touch pen Sheng agricultural chemicals container In the model. Use the inert gas (nitrogen) to pressurize the type for 6 seconds to 100%. Next, lower the contents of the container and degas the meter for 5 seconds. Subsequently, the vessel was repressurized with a reactive rolling stock containing nitrogen and 1 to 10% of fluorine gas for a period of 6 seconds to about 丨(9) cc/square 忖 (^7 MPa). Thereafter, the force is released and the container is degassed for a second. 4, re-pressurize the container with inert nitrogen for 6 seconds to about (10) broken / square inch ^ 〇 · 7 MPa) (four). Thereafter, the force was released and the container was degassed for 5 seconds. After the extraction, the inert nitrogen gas is used to repressurize the vessel for 6 seconds to about 1 lb./sq. ft. (0.7-MPa). Thereafter, the container is returned to the atmosphere and removed from the mold. The resulting molded container contained an inner wall having a 氟2_thick fluorine coating. Experimental Example a) Liquid-blocking toluene, Desys herbicide (!% deltamethrin + emulsifier, stabilizer and solvent; KyungNong), Bats^ insecticide (50/. BpMC + 5〇) The %2 emulsifier and solvent) and water were placed in the containers manufactured in Examples 1 to 6 and Comparative Examples 丨 to 3. Next, after 3 days, the weight change was measured under forced discharge conditions at 50 °C. For toluene, the change in weight was further measured at room temperature. 26 1320771 18784pif.doc b ) Gas barrier (cubic centimeters per square meter · day · atmospheric pressure (cc / m2. day · atm)) at temperatures of 23 ° C and 50% relative humidity, examples 1 to 6 and The containers prepared in Comparative Examples 1 to 3 were placed separately for 1 day. Next, the gas permeability (MoconOX-TRAN 2/20, U.S.A.) was measured.

表1 氣體阻絕性 氧氣穿透 (平方公分/平方 米· 24小時·大氣 壓力(cm2/m2.24 hrs · atm )) 濕氣穿透 (克/平方米·24 小時(g/m2-24 hrs )) 實例1 5.3 1.04 實例2 2.5 1.05 實例3 9.6 0.98 實例4 -1.83 1.01 實例5 11.1 1.02 實例6 1.96 1.02 比較實例1 35.4 1.32 比較實例2 34.8 1.26 比較實例3 56.4 2.03 27 18784pif.doc 表2 分類 液體阻絕性 ^液體阻絕性 〜於Table 1 Gas barrier oxygen breakthrough (square centimeters / square meter · 24 hours · atmospheric pressure (cm2 / m2.24 hrs · atm)) moisture penetration (g / square meter · 24 hours (g / m2-24 hrs )) Example 1 5.3 1.04 Example 2 2.5 1.05 Example 3 9.6 0.98 Example 4 -1.83 1.01 Example 5 11.1 1.02 Example 6 1.96 1.02 Comparative Example 1 35.4 1.32 Comparative Example 2 34.8 1.26 Comparative Example 3 56.4 2.03 27 18784pif.doc Table 2 Classification Liquid Resistive liquid resistance

於25¾ 的重量 變化Weight change at 253⁄4

_實例g 實例3 0.008 ^088^18?_Instance g Instance 3 0.008 ^088^18?

比較實 例1 0.430 4.593 例2 比較實 例3Comparative Example 1 0.430 4.593 Example 2 Comparative Example 3

6.3046.304

Desys 0.105 0.061 0.091 0.052 0.094 0.054 1.126 1.312 1.638Desys 0.105 0.061 0.091 0.052 0.094 0.054 1.126 1.312 1.638

如表1及2戶斤- ^ /s, , _ $’相較於比較實例1 5 〇 見例1至6之容器,至3之彼等容器 本發明之JLh I 錢随絕性。 产.月之具有阻絕性之物品具有優良的 氧、有機溶劑及濕氣職強的阻絕。㈣械強度以 雖然本發明已以較佳實施例揭露如上,然.並 限定本發明,任何熟習此技藝者,在不脫離本發明之精_ 28 1320771 18784pif.doc 和範圍内,當可作些許之更動與潤飾,因此本發明之保護 範圍當視後附之申請專利範圍所界定者為準。 【圖式簡單說明】 無 【主要元件符號說明】 無As shown in Tables 1 and 2, - ^ /s, , _ $' compared to the comparative example 1 5 见 See the containers of Examples 1 to 6, to the containers of 3, the JLh I of the present invention is absolute. Products with resistance to the month of the month have excellent resistance to oxygen, organic solvents and moisture. (4) Mechanical strengths Although the present invention has been disclosed in the preferred embodiments as above, and the present invention is defined, any person skilled in the art can make a few changes without departing from the scope of the invention _ 28 1320771 18784pif.doc The scope of protection of the present invention is defined by the scope of the appended claims. [Simple diagram description] None [Main component symbol description] None

2929

Claims (1)

1320771 修正日期:97年7月3丨日 號中文專利範圍無劃線修正本 十、申請專利範圍: 1.種具有阻絕性的物品,具有一氟塗覆内壁,且由 乾混合組合物製備,該具有阻絕性的物品包含: 40至96重量份的聚烯烴樹脂; 乎份喊雜紐H域合物,該奈 :黏土及具有阻絕性的至少-樹脂,該 乙=所Γί 歸醇共聚物、聚酿胺、離子聚合物及聚 乙烯醇所組成之族群;以及 1至30重量份的相容劑, = t複合物中具有阻絕性之該樹紗該插入黏 土的重里比為 58.0 : 42.0 至 99.9 : 0.1, 其中該相容劑為選自由乙烯_乙烯& 丙烯酸乙酉旨共聚物、乙稀·丙稀酸貌基酉旨_㈣酉1丘聚 =、順^二酸酐改質(接枝)高密度聚乙締、順丁婦= 酉夂酐改質(接枝)直鏈低密度聚乙烯、乙婦其 酸炫基醋-(曱基)丙烯酸共聚物、乙婦-丙稀酸^卒 物、乙烯·乙酸乙_共聚物、順谓二酸酐 乙烯-乙酸乙烯酯共聚物所組成之族群中之―或户1接技_) 物, I 口 1匕兮^ 其中該具有阻絕性的物品為容器、膜、 其中該氟塗覆内壁之塗層之厚度為00 I 2.如申請專利範圍第I項所述之且 以111。 其中該插人黏土為選自由蒙脫土、膨潤土、的物品, 裡息石、氟代財石、m得石、綠:^石母、 30 1320771 18784pif.doc 蛭石、多水高嶺土、唯康土、沙康土、馬吉土及肯尼土所 組成之族群的至少一化合物。 3. 如申請專利範圍第1項所述之具有阻絕性的物品, 其中該插入黏土包含1至45重量%之一有機材料。1320771 Revision date: July 3, 1997 Japanese patent range without slash correction This ten, the scope of patent application: 1. A kind of barrier-resistant article, with a fluorine coated inner wall, and prepared from dry mixed composition, The barrier article comprises: 40 to 96 parts by weight of a polyolefin resin; a heterogeneous H-domain complex, the naphthalene: clay and at least a resin having a barrier property, the B = Γ a group consisting of a polyamine, an ionic polymer, and a polyvinyl alcohol; and 1 to 30 parts by weight of a compatibilizing agent, which has a barrier property in the = t composite. The weight ratio of the inserted clay to the clay is 58.0 : 42.0 To 99.9 : 0.1, wherein the compatibilizer is selected from the group consisting of ethylene-ethylene & ethyl acrylate copolymer, ethyl acetoacetate, _ (four) 酉 1 yam == cis dianhydride Branch) high-density polyethylene, cis-butan = phthalic anhydride modified (grafted) linear low-density polyethylene, ethoxylated acid vinegar-(mercapto)acrylic acid copolymer, ethyl-acrylic acid ^Astrology, ethylene·acetic acid B-copolymer, cis-dianhydride ethylene-vinyl acetate In the group consisting of copolymers, or the household 1 _ _ _ 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 2. As stated in item I of the patent application and at 111. The inserted clay is selected from the group consisting of montmorillonite and bentonite, lining stone, fluoridated fossil, m stone, green: ^ stone mother, 30 1320771 18784pif.doc vermiculite, multi-water kaolin, Weikang At least one compound of the group consisting of earth, Shakang soil, Magi soil, and Kenney soil. 3. The article of the invention of claim 1, wherein the insert clay comprises from 1 to 45% by weight of an organic material. 4. 如申請專利範圍第3項所述之具有阻絕性的物品, 其中該有機材料具有至少一官能基,該官能基選自由··一 級録至四級録、鱗、順丁烯二酸醋、破拍酸醋、丙缚酸醋、 苯曱基氫、噁唑啉及二曱基二硬脂醯銨。 5. 如申請專利範圍第1項所述之具有阻絕性的物品, 其中該乙烯·乙烯醇共聚物含有1〇至50莫耳%之乙稀。 6. 如申凊專利範圍第1項所述之具有阻絕性的物品, 其中該聚胺為耐論4.6、耐論6、财給6.6、耐論6.10、 而才論7、耐綸8、耐論9、财綸11、对綸12、耐論46、MXD6、 非晶系聚醯胺、含有至少兩個該聚醯胺之共聚合聚醯胺或 至少兩個該聚酿胺之混合物。4. The article of claim 3, wherein the organic material has at least one functional group selected from the group consisting of a first grade to a fourth grade, a scale, a maleic acid vinegar. Broken sour vinegar, acenaphthyl vinegar, benzoyl hydrogen, oxazoline and dinonyl distearyl ammonium. 5. The article of the invention of claim 1, wherein the ethylene vinyl alcohol copolymer contains from 1 to 50 mol% of ethylene. 6. For example, the article having the resistive property mentioned in Item 1 of the patent scope, wherein the polyamine is resistant to 4.6, resistant to theory 6, financial to 6.6, resistant to 6.10, and only to 7, nylon 8, resistant On the basis of 9, 9, or 12, MXD6, amorphous polyamine, a copolymerized polyamine containing at least two of the polyamines or a mixture of at least two of the polyamines. 7. 如申請專利範圍第6項所述之具有阻絕性的物品, 其中該非晶系聚醯胺的玻璃態轉換溫度為約8〇·13〇ΐ:。 8. 如申請專利範圍第6項所述之具有阻絕性的物品, 其中該非晶系聚軸是選自由己二胺間苯二曱酿胺;呈有 ,至議〇之間苯二曱酸/對苯二曱酸之比率的己二胺間 本-曱ϋ胺/對苯二曱醯胺三元共聚物;2 2 4• 一 胺對苯二甲蕴胺盘2 4 4-二甲其p ’ ’ 土一 合物:以及己二胺或2:甲;曱戊基=笨之混 甲酸或其混合物之共聚物所二甲酸、對笨二 31 1320771 18784pif.doc 項所述之具有阻絕性的物品, 八中該非日0絲_為具有7〇:3 甲酸之比率的己二胺間苯 =一甲酉夂比對本― 聚物。 羯胺/對未二甲酿胺三元共 10.如申請專利範圍第1 品,其中該離子聚合物具有每10分絕性的物 指數(190°c, 2,160克)。 刀,,里.至10克之熔融 法,^種製造具有阻絕性及氟塗覆㈣之物品的方 藉由乾混合40至96 #旦八 重量份之具有阻絕性的奈米二二〇.5至60 黏土及至少一種選自=;物乙:奈= 合物包含-插入 聚合物及聚乙稀醇所_ ㈣料物、聚_、離子 模製該奈米複合物性的樹脂; 二氣塗覆,物品的一内壁场成物…及 氟塗覆利範圍第11項所述之製造具有阻絕性及 塗覆。^物,方法,其巾制^作成形法純 氟塗覆利範圍第11項所述之製造具有阻絕性及 力口壓成#/ ·+、6 °D的方法,是經由吹塑成形、掩壓成形、 遂成形或料柄彡來製造。 土祕 m 327. The article of the invention of claim 6, wherein the amorphous polyamine has a glass transition temperature of about 8 〇 13 〇ΐ:. 8. The article of the invention of claim 6, wherein the amorphous polyaxial axis is selected from the group consisting of hexamethylenediamine and benzoic acid/ The ratio of p-diamine to hexamethylenediamine/p-benzoguanamine terpolymer; 2 2 4• monoamine p-terephthalic acid disk 2 4 4-dimethyl-p ' ' soil mono-compound: and hexamethylene diamine or 2: A; 曱 pentyl = stupid mixed formic acid or a mixture of the copolymer of dicarboxylic acid, as described in the block diagram of 31 1320771 18784pif.doc The article, the eight-day non-Japanese 0 wire _ is a ratio of hexamethylenediamine benzene = one formazan with a ratio of 7 〇:3 formic acid. Indoleamine/p-dimethylamine ternary 10. As claimed in the patent scope, the ionic polymer has an index of extinction per 10 minutes (190 ° C, 2,160 g). Knife,, in. to 10 grams of melting method, the production of materials with barrier and fluorine coating (four) by dry mixing 40 to 96 #旦eight parts by weight of the barrier nano 2D.5 Up to 60 clay and at least one selected from the group consisting of:; B: Nai compound comprising - inserting polymer and polyethylene glycol - (4) material, poly-, ion-molding the nano-composite resin; The coating, an inner wall field of the article... and the fluorine coating range 11 manufactured are resistant to coating and coating. ^Method, method, method for forming a pure fluorine coating according to item 11 of the invention, which has the properties of resistive and force-pressing into #/·+, 6 °D, is formed by blow molding, Manufactured by mask forming, 遂 forming or 料. Earth secret m 32
TW094142900A 2004-12-07 2005-12-06 Article having high barrier property TWI320771B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR20040102214 2004-12-07
KR1020050033527A KR100724552B1 (en) 2004-12-07 2005-04-22 High barrier goods

Publications (2)

Publication Number Publication Date
TW200621871A TW200621871A (en) 2006-07-01
TWI320771B true TWI320771B (en) 2010-02-21

Family

ID=37159544

Family Applications (1)

Application Number Title Priority Date Filing Date
TW094142900A TWI320771B (en) 2004-12-07 2005-12-06 Article having high barrier property

Country Status (3)

Country Link
KR (1) KR100724552B1 (en)
CN (1) CN101001906A (en)
TW (1) TWI320771B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9902854B2 (en) * 2015-12-14 2018-02-27 Hyundai Motor Company Polyamide composite resin composition for fuel filler pipe

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4197784B2 (en) 1998-11-24 2008-12-17 横浜ゴム株式会社 Thermoplastic elastomer composition excellent in gas barrier property and laminate using the same
KR100551135B1 (en) 1999-03-09 2006-02-10 주식회사 새 한 Manufacturing method of anti-reflective transparent sheet having excellent antifouling properties
KR100508907B1 (en) 2001-12-27 2005-08-17 주식회사 엘지화학 Nanocomposite blend composition having super barrier property

Also Published As

Publication number Publication date
TW200621871A (en) 2006-07-01
KR100724552B1 (en) 2007-06-04
KR20060063569A (en) 2006-06-12
CN101001906A (en) 2007-07-18

Similar Documents

Publication Publication Date Title
AU2005202978B2 (en) Nanocomposite composition having super barrier property and article using the same
TWI292418B (en) Nanocomposite composition having high barrier property
AU2005264685B2 (en) Gas-barrier nanocomposite composition and article using the same
AU2005310435B2 (en) Article having barrier property
US20060121224A1 (en) Article having high barrier property
JP2008518076A (en) Barrier tube container
KR101002050B1 (en) Barrier multilayer articles
KR100874031B1 (en) Nanocomposite compositions with excellent barrier properties and articles made therefrom
TWI328592B (en) Gas-barrier nanocomposite composition and article using the same
TWI320771B (en) Article having high barrier property
KR100789240B1 (en) Blocking Nanocomposite Compositions and Articles Using the Same
TW200409796A (en) Nanocomposite blend composition having super barrier property