TW200932476A - Process for producing injection-molded article and masterbatch for use in the same - Google Patents

Process for producing injection-molded article and masterbatch for use in the same Download PDF

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TW200932476A
TW200932476A TW97144649A TW97144649A TW200932476A TW 200932476 A TW200932476 A TW 200932476A TW 97144649 A TW97144649 A TW 97144649A TW 97144649 A TW97144649 A TW 97144649A TW 200932476 A TW200932476 A TW 200932476A
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resin
mass
cyclic olefin
molecular weight
cyclic
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TW97144649A
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Chinese (zh)
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TWI448373B (en
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Miyazaki Hirotaka
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Polyplastics Co
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/22Compounding polymers with additives, e.g. colouring using masterbatch techniques
    • C08J3/226Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L45/00Compositions of homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic ring system; Compositions of derivatives of such polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/0001Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor characterised by the choice of material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2345/00Characterised by the use of homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic ring system; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2445/00Characterised by the use of homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic ring system; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

A process for producing an injection-molded article. The process facilitates injection molding while taking advantage of the features of a low-molecular cycloolefin resin. Also provided is a masterbatch for use in the process. A masterbatch comprising a cycloolefin resin and a low-molecular cycloolefin resin having a number-average molecular weight of 10,000 or lower and a cycloolefin resin are dry-blended and then injection-molded. The masterbatch preferably comprises 20-95 mass% the cycloolefin resin and 5-80 mass% the low-molecular cycloolefin resin.

Description

200932476 九、發明說明: 【發明所屬之技術領域】 本發明係關於使用低分子量環狀烯烴系樹脂之射出成 形品的製造方法以及用於此的含有低分子量環狀稀烴系樹 脂之高濃度染色配料。 【先前技術】 環狀烯烴系樹脂’由於透明性、对藥品性、防濕性、 ® 機械特性等優良,故用於作為光學用途、及醫藥或者醫療 機器用途等的材料。又,環狀烯烴系樹脂,熔融加工性及 流動性亦優良,亦利用在膜狀或者片狀的成形品、及包裝 材料。再者,環狀烯烴系樹脂的熱收縮性及印刷特性亦優 良。如此地,環狀烯烴系樹脂被使用於各式各樣的領域。 又,環狀烯烴系樹脂,除了如上所述有用之面之外, 在熔融成形時有產生凝膠狀物而使成形表面粗糙降低外觀 ◎ 特性之面。該外觀特性的下降,特別在利用環狀烯烴系樹 .脂作為透明㈣、先學用途、包裝材料時會造成很大的影 響。 為解決上述外觀特性的下降,於專利文獻丨揭示有藉 由調合高分子量環狀烯烴系樹脂及低分子量環狀稀烴系樹 月旨’即使溶融成形’亦可使成形品的表面變得平滑的技術。 [專利文獻1 ]國際公開W02007/132641號小冊 .【發明内容】In the present invention, the present invention relates to a method for producing an injection molded article using a low molecular weight cyclic olefin resin and a high concentration dyeing of the low molecular weight cyclic rare hydrocarbon resin used therefor. Ingredients. [Prior Art] The cyclic olefin resin is excellent in transparency, chemical properties, moisture resistance, and mechanical properties, and is used as a material for optical applications, medical applications, medical applications, and the like. Further, the cyclic olefin resin is excellent in melt processability and fluidity, and is also used in a film-like or sheet-like molded article and a packaging material. Further, the cyclic olefin resin is excellent in heat shrinkability and printing properties. As described above, the cyclic olefin resin is used in various fields. Further, the cyclic olefin-based resin has a gel-like substance formed during melt molding, and the surface of the cyclic olefin-based resin is roughened to lower the appearance of the surface. This decrease in the appearance characteristics is particularly affected by the use of a cyclic olefin-based resin as a transparent (four), a prior learning application, and a packaging material. In order to solve the above-described deterioration in the appearance characteristics, it is disclosed in the patent document that the surface of the molded article can be smoothed by blending a high molecular weight cyclic olefin resin and a low molecular weight cyclic rare hydrocarbon tree. Technology. [Patent Document 1] International Publication WO2007/132641 Booklet. [Summary of the Invention]

2254-1 〇158-PF 5 200932476 [發明所欲解決的課題] 巧、::度ί於樹脂成形’常使用能以-步驟將複雜、精 出成J 可以短時間完成成形品的射出成形法。射 出成形法,可以加工曰用品、 骨& _ %々 €軋裏°〇的零件、汽車用的 零件夕種多樣的材料。又,最近模 取跹禊具構造的複雜化、精巧 化、零件的集約化,零件一 ..^ 體化破進行,使得非以射出 成形不可的零件變多。 =是,根據專利文獻!的發明,使用低分子量環狀稀煙 系樹月曰及環狀烯烴系榭脂作发 系樹月曰作為成形材料射出成形,則樹脂 = 义入性不佳,而計量時間會變長。目此,以專利文獻i 法’成形材料在每次成形的供料需時,而降低生產性。 又’在低分子量環狀締煙系樹腊及環狀稀烴系樹脂之熔 融’則會在每次成形的供應量及計量時間發生離散而使成 :品的品質變的不隱定。因此,要求可有效地利用低分子 量環狀稀㈣樹脂特徵,且可容易地射出成形成的技術。 本發明係為解決如上課題而完成者,其目的係在於提 供可有效地利用低分子量環狀烯烴系樹脂之特徵,且可容 易地射出成形的技術。 [用以解決課題的手段] 本發月者們4解決上述課題專心反覆研究。其結果 發明者們發現,藉由將包含環狀烯煙系樹脂及數目平均分 量為1 0000以下的低分子量環狀烯烴系樹脂的高濃度染 色配料;及環狀烯烴系樹脂,在乾燥混合後後射出成形, 可容易地做射出成形’ π完成本發I更具體而,言,本發 2254-1〇158科 200932476 明提供如下者。 (1)一種射出成形品的製造方法,其係使用環狀烯烴系 樹脂;及數目平均分子量1()_以下的低分子量環狀稀煙系 樹脂之射出成形品的製造方法,其係在將高濃度染色配 料其包含環狀烯煙系樹脂及低分子量環狀婦煙系樹脂; 及環狀烯烴系樹脂乾燥混合後射出成形。 ❹ ❹ :據⑴的發明,可容易地得到高品質的射出成形品。 如先前,未將低分子量環狀蝉烴系樹月旨高濃度染色配料化 而使用,則玻璃轉移溫度低,因分子量低而使朦粒非常的 脆’會因可塑化時的壓縮或摩擦而容易粉碎成粉而附著於 基底的膠粒表面。因該粉的影響使可塑化前半的固體在運 輸時與料管的摩擦變小而咬入品質變差。再者’低分子量 環狀烯烴系樹脂迅速地熔融,呈低黏度狀態。樹脂與螺桿 之,擦係數,隨著接近樹脂與料管的摩擦係數,樹脂變的 不谷易被輸送到前方,再者如果樹脂與螺桿的摩擦係數, 超過樹脂與料管的摩擦係數,則樹脂將無法被輸送到前 方。因此,如果不將抵分子量環狀烯烴系樹脂高濃度染色 配料化使用,則在樹脂對螺桿的咬入性將產生問題。在本 發明’藉由,低分子量環狀烯烴系樹脂高濃度染色配料化 而使用’使南漠度染色配料的破璃轉移溫度較低分子量環 狀烯烴系樹脂玻螭轉移溫度為低、又,提升膠粒的韌性, 即使有可塑化時的屡输;^ B ^ 町町縻縮及摩擦,亦不易成粉,故可抑制迅 速的熔融,改善樹脂的咬入性。 ⑵⑴所述的射出成形品的製造方法,其中上述高濃2254-1 〇 158-PF 5 200932476 [Problems to be Solved by the Invention] Ingeniously:: Degrees of resin molding 'usually can be used in a step-by-step process that can be complicated and refined into J. The injection molding method can be completed in a short time. . In the injection molding method, it is possible to process a variety of materials such as parts for enamel products, bones, _% 々 轧 轧, and parts for automobiles. In addition, the complexity of the mold structure, the intensiveness of the parts, and the intensification of the parts have recently been carried out, so that the parts that are not formed by injection molding are increased. = Yes, according to the patent literature! According to the invention, the low molecular weight cyclic smoky tree sap and the cyclic olefin saponin are used as the molding material for injection molding, and the resin = poor input property, and the measurement time becomes long. Therefore, in the patent document i method, the forming material takes time for each forming of the forming material, and the productivity is lowered. Further, the melting of the low-molecular-weight cyclic flue-cured wax and the cyclic dilute-based resin is discrete in the supply amount and the measurement time of each molding, and the quality of the product is not determined. Therefore, it is required to be able to effectively utilize low molecular weight cyclic dilute (tetra) resin characteristics and to easily form a technique for formation. The present invention has been made to solve the above problems, and an object of the present invention is to provide a technique capable of effectively utilizing a low molecular weight cyclic olefin-based resin and easily ejecting and molding. [Means to solve the problem] This month's people 4 solve the above problems and concentrate on repeated research. As a result, the inventors have found that a high-concentration dyeing ingredient containing a cyclic olefin-based resin and a low-molecular-weight cyclic olefin-based resin having a number average component of 100,000 or less and a cyclic olefin-based resin are dried and mixed. After the injection molding, the injection molding can be easily performed. π Completion of the present invention is more specific, and the present invention is provided by the following 2254-1〇158 Section 200932476. (1) A method for producing an injection molded article, which comprises using a cyclic olefin resin; and a method for producing an injection molded article of a low molecular weight cyclic thinning resin having a number average molecular weight of 1 () or less, which is The high-concentration dyeing ingredient comprises a cyclic olefinic resin and a low molecular weight cyclic vodonic resin; and the cyclic olefin resin is dried and mixed, and then injection molded. ❹ ❹ According to the invention of (1), a high-quality injection molded article can be easily obtained. As in the past, when the low-molecular-weight cyclic terpene hydrocarbon tree is not used for the high-concentration dyeing, the glass transition temperature is low, and the granules are very brittle due to the low molecular weight, which is caused by compression or friction during plasticization. It is easy to pulverize into powder and adhere to the surface of the rubber particles of the substrate. Due to the influence of the powder, the friction of the first half of the plasticizable body with the material tube during transportation becomes small and the biting quality is deteriorated. Further, the low molecular weight cyclic olefin resin rapidly melts and exhibits a low viscosity state. Resin and screw, the coefficient of friction, as the coefficient of friction between the resin and the tube is close to the resin, the resin is not transported to the front, and if the coefficient of friction between the resin and the screw exceeds the coefficient of friction between the resin and the tube, The resin will not be transported to the front. Therefore, if the high-density dyeing of the molecular weight cyclic olefin-based resin is not used for dyeing, there is a problem in the biting property of the resin to the screw. In the present invention, by using a low-molecular-weight cyclic olefin-based resin for high-concentration dyeing and dosing, the use of a low-molecular-weight cyclic olefin-based resin glass transition temperature of a low-molecular-weight dyeing ingredient is low, and It improves the toughness of the rubber pellets, and it is easy to lose even if it is plasticized. ^ B ^ Machimachi shrinks and rubs, and it is not easy to form powder, so it can suppress rapid melting and improve the biting property of the resin. (2) The method for producing an injection-molded article according to (1), wherein the above-mentioned high concentration

2254-1015S-PF 200932476 度染色配料係由環灿、法,ηγ< ^ . m栖八;甚量為20質量%至95質量 〇/έή ^^ ^ , 僻枷含重係為5質量%至80質量 辰度染色配料’於上述乾燥混合之步驟,對上述環狀 烯烴系樹脂100質量邻,# μ、+、^_ β 奵上述環狀 負重邛,使上述高濃度染色 至100質量部的混合物。 针马5質量邻 根據(2 )的發明,藉由蔣 上述範圍含有,只要是低八^成的Μ度染色配料以 要疋低刀子量環狀烯烴 狀烯烴系樹脂之量等同亦以:+ 衝伽之量與環 以〜“ 高Μ染色配料縣將且 性’而有粉的產生量小且不容易引起計量問題 項所射種屮高:度染色配料’其係用於⑴或⑵之任何- 祕,Γ Ji t形品的製造方法之高濃度染色配料,環狀 烯烴系樹脂含量為20質量%至 / 5質量% ’上述低分子晉環站 烯烴系樹脂含量為5質量%至8。質量-刀子量環狀 (4) (3)所述的高濃度染色配 ❹ 狀烯烴系樹脂含量為1〇質量%至70質量:。上述低分子量環 根據(3)、(4)的發明,藉 脂含量在上述範圍,可改上由:低分子量環狀晞烴系樹 地控制凝膠的發生。因此, 並且了充刀 品質的射出成形品。 了進-步以高的生產性製造高 (5) (3)或(4)所述的高道;九 度為100°C以下。 又木色配料’其中玻璃轉移溫 根據(5)的發明,由於言、、曾电 A 1 Π Π °r T m , 又乐色配料的玻璃轉移溫度 為100C以下,因此熔融成形 ^ 度 、候’尚濃度染色配料較環.2254-1015S-PF 200932476 degree dyeing ingredients are from the ring can, the law, ηγ < ^ . m habitat eight; the amount is 20% by mass to 95 mass 〇 / έή ^ ^ ^, the secluded weight system is 5% by mass to 80 mass of dyeing ingredients 'in the above-mentioned dry mixing step, the above cyclic olefin resin 100 mass adjacent, # μ, +, ^_ β 奵 the above-mentioned cyclic load 邛, so that the above high concentration dyeing to 100 mass parts mixture. According to the invention of (2), the needle is contained in the above range, and as long as it is a low-grade dyeing ingredient, the amount of the cyclic olefin-like olefin resin is required to be reduced by the same amount: + The amount of rushing and the ring is ~"" sorghum dyeing ingredients will be sex" and the amount of powder produced is small and it is not easy to cause the measurement problem item to be high: the dyeing ingredient 'is used for (1) or (2) Any of the high-concentration dyeing ingredients of the manufacturing method of the ji-shaped product, the content of the cyclic olefin resin is 20% by mass to 5% by mass. The above-mentioned low molecular weight Jinhua station olefin resin content is 5% by mass to 8 The mass-knife amount ring (4) (3) The high-concentration dyeing and the olefin-like resin content is from 1% by mass to 70% by mass. The above-mentioned low molecular weight ring is in accordance with the inventions of (3) and (4). In the above range, the fat content can be changed from the low molecular weight cyclic terpene hydrocarbon tree to control the occurrence of the gel. Therefore, the injection molded product of the filling quality is produced. The production is advanced with high productivity. High (5) (3) or (4) high road; nine degrees below 100 ° C. 'The glass transfer temperature according to the invention of (5), because of the words, the electricity of A 1 Π Π °r T m , and the glass transition temperature of the music color ingredients is below 100C, so the melt forming degree, the temperature of the dyeing The ingredients are more than the ring.

2254-10158-PF 200932476 狀烯烴系樹脂會先熔化,可使環狀烯烴系樹脂所受剪力 小。因此可更有效地抑制凝膠狀物的產生。 [發明效果] 根據本發明,藉由將高濃度染色配料,其 一 0左壤狀晞 煙系樹脂及數目平均分子量為1 0000以下的低分子量環狀 烯烴系樹脂;及環狀烯烴系樹脂,於乾燥混合步驟後射出 成形’可有效地利用低分子量環狀烯烴系樹脂之特徵,容 易地獲得高品質的射出成形品。 Ο 【實施方式】 以下詳細地說明關於本發明的實施形態。本發明並非 限定於以下的實施形態’在本發明的目的的範圍内,可適 宜加以變更實施。再者關於說明反覆之處,有適宜將說明 省略之情形,並非限定發明的要旨者。 本發明係將高濃度染色配料’其包含環狀烯烴系樹脂 及數目平均分子量為1 0000以下的低分子量環狀烯烴系樹 脂;及環狀烯烴系樹脂,乾燥混合步驟後射出成形之射出 成形品之製造方法及用於此的高濃度染色配料。本發明之 特徵在於:使用包含環狀烯烴系樹脂及數目平均分子量為 1 00 00以下的低分子量環狀烯烴系樹脂的高濃度染色配料。 用於本發明之南濃度染色配料,包含環狀稀烴系樹脂 及數目平均分子量為1 0000以下的低分子量環狀烯烴系樹 脂。 *〈環狀烯烴系樹脂〉 2254-1015B-PF 9 200932476 以下,說明以本發明製造的射出成形品以及本發明的 冋;辰度木色配料的必須成分的環狀烯烴系樹脂。使用於本 發明之環狀稀煙系樹脂,係包含環狀烯烴成分作為共聚合 成分者,只要是在主鏈包含環狀烯烴成分的聚烯烴系樹 脂,並無特別限定。可舉例如 (al)環狀烯烴的加成聚合物或其加氫物。 (a2)環狀烯烴及α—烯烴加成共聚物或其加氫物。2254-10158-PF 200932476 The olefin-based resin is first melted, and the cyclic olefin resin can be subjected to a small shear force. Therefore, the generation of the gel can be suppressed more effectively. [Effect of the Invention] According to the present invention, a high-concentration dyeing ingredient is a low-molecular-weight cyclic olefin resin having a number average molecular weight of 1,000,000 or less and a cyclic olefin resin, and a cyclic olefin resin. After the drying and mixing step, the injection molding can effectively utilize the characteristics of the low molecular weight cyclic olefin resin, and a high-quality injection molded article can be easily obtained.实施 Embodiments Hereinafter, embodiments of the present invention will be described in detail. The present invention is not limited to the following embodiments, and can be appropriately modified and implemented within the scope of the object of the present invention. In addition, in the case where the explanation is repeated, it is appropriate to omit the description, and it is not intended to limit the gist of the invention. The present invention relates to a high-concentration dyeing ingredient comprising a cyclic olefin-based resin and a low-molecular-weight cyclic olefin-based resin having a number average molecular weight of 1,000,000 or less; and a cyclic olefin-based resin, which are injection-molded by injection molding after drying and mixing steps. The manufacturing method and the high concentration dyeing ingredients used therefor. The present invention is characterized in that a high-concentration dyeing ingredient comprising a cyclic olefin-based resin and a low molecular weight cyclic olefin-based resin having a number average molecular weight of 1,000,000 or less is used. The south concentration dyeing ingredient used in the present invention comprises a cyclic dilute resin and a low molecular weight cyclic olefin resin having a number average molecular weight of 1,000,000 or less. * "Cyclic olefin-based resin" 2254-1015B-PF 9 200932476 Hereinafter, a cyclic olefin-based resin which is an essential component of the injection-molded article produced by the present invention and the enamel-tune wood-colored component of the present invention will be described. The cyclic thin-type resin to be used in the present invention is a polyolefin-based resin containing a cyclic olefin component as a copolymer component, and is not particularly limited as long as it is a polyolefin-based resin containing a cyclic olefin component in the main chain. For example, an addition polymer of (al) a cyclic olefin or a hydrogenated product thereof can be mentioned. (a2) a cyclic olefin and an α-olefin addition copolymer or a hydrogenated product thereof.

❹ U3)環狀烯烴開環(共)聚合物或其加氫物。 又,包含用於本發明之環狀烯烴成分作為共聚合成分 之環狀烯烴系樹脂,有 U4)對上述(al)〜(a3)的樹脂,接枝及/或共聚合具有 極性基的不飽和化合物者。 極性基’可舉例如缓基、酸野基、環氧基、酿胺基、 S曰基羥基等,有極性基的不飽和化合物,可舉(甲基)丙 稀酸、馬來酸、馬來酐、衣康肝、縮水甘油基(甲基)丙稀 酸醋、(甲基)丙稀酸院基(碳數卜⑼醋、馬來酸垸基(碳數 1~10)醋、(曱基)丙烯醯胺、(甲基)丙烯酸_2_經基乙酯等。 在;本發明,包含上述環狀烯烴成分作為共聚合成分 的環狀婦烴系樹脂(al)训,可以單m種或混合二種 以上使用。 已3用於本發明之環狀烯烴成分作為共聚合成分 之環狀烯烴系樹脂,亦可使用市售之樹脂。市售之環狀烯 煙系樹脂’可舉例如,聰s(註冊商標)(聰s騰聽 POLYMER公司製)、舰(註冊商標)(三井化學公司製卜❹ U3) a cyclic olefin ring-opening (co)polymer or a hydrogenated product thereof. Further, the cyclic olefin resin containing the cyclic olefin component of the present invention as a copolymerization component has U4) a resin having the polar group in the above (al) to (a3) resins, and grafting and/or copolymerization. Saturated compound. Examples of the polar group include, for example, a slow group, an acid group, an epoxy group, an amine group, a S-mercapto group, and the like, and a polar group-containing unsaturated compound, and examples thereof include (meth)acrylic acid, maleic acid, and horse. Anhydride, Yi Kang liver, glycidyl (meth) acrylate vinegar, (meth) acrylic acid hospital base (carbon number (9) vinegar, maleic acid sulfhydryl (carbon number 1 ~ 10) vinegar, (曱 ) 醯 醯 ) 醯 、 醯 醯 醯 醯 醯 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状 环状In the case of the cyclic olefin resin which is used as the copolymer component in the cyclic olefin component of the present invention, a commercially available resin may be used. A commercially available cyclic olefinic resin may be used. For example, Cong S (registered trademark) (Cong Seng listens to POLYMER company), ship (registered trademark) (Mitsui Chemical Co., Ltd.)

2254-10158-PF 200932476 ΖΕ0ΝΕΧ(註冊商標)(日本ΖΕΟΝ公司製)、ZE0N0R(註冊商 標)(日本ΖΕΟΝ公司製)' ART0N(註冊商標)(jsR公司製)等。 可良好地使用於本發明的組成物的(a2)環狀烯烴及a-烯烴加成共聚物,並無特別限定。特別良好的例,可舉包 含[1]碳數2〜20之α-烯fe成分;及[2]以下述通式(I)表示 的環狀烯烴成分的共聚物。2254-10158-PF 200932476 ΖΕ0ΝΕΧ (registered trademark) (manufactured by Nippon Co., Ltd.), ZE0N0R (registered trademark) (manufactured by Nippon Co., Ltd.) ' ART0N (registered trademark) (manufactured by JsR Co., Ltd.). The (a2) cyclic olefin and the a-olefin addition copolymer which can be suitably used in the composition of the present invention are not particularly limited. Particularly preferred examples thereof include a copolymer of a cyclic olefin component represented by the following formula (I): [1] an α-ene fe component having 2 to 20 carbon atoms; and [2].

❺ ❹ * * * (I ) (式中m分別相同亦可不同,係選自錢 齒素原子以及烴基所組成之群、也可以將aRie、R -體化形成二價的碳氫基’“^"及〜相互 又,η係表示0或正的整數,瞒2以上時,成環。 的單位之中,分別可相同亦可不同。) 反覆 [[1]碳數2〜20之α-烯烴成分] 可良好地使用於本發明 稀等其他*聚合成分之加成:::二成分及可成為與己 2〜20之烯烴,並盔 “聚合成分之碳數 I…狩別限定。可舉你 丁烯' 1-戊烯、1-己稀、3 , 烯、卜 1 Τ暴一I —丁熵、q田盆, 3-乙基-1-戊烯、4_甲 甲基―1〜戊烯、 44 τ 1-1-戊烯、4_ 二甲基-1-己烯、4,4-_甲某彳a 土 烯、4,4〜 ,a —甲基~卜戊烯、4 乙基-卜己蝉、卜辛烯、卜癸稀 歸、3〜 十一碳烯、卜十四唆烯、❺ ❹ * * * (I ) (wherein m may be the same or different, selected from the group consisting of a dentate atom and a hydrocarbon group, or aRie, R - may be formed to form a divalent hydrocarbon group'" ^" and ~ mutually, η means 0 or a positive integer, 瞒2 or more, into a ring. The units can be the same or different.) Repeat [[1] carbon number 2~20 α -Olefin component] It can be suitably used for the addition of other *polymerizable components such as dilute in the present invention:: two components and an olefin which can be 2 to 20, and the helmet "the carbon number of the polymerization component I is limited." It can be mentioned that your butene ' 1-pentene, 1-hexene, 3, ene, Bu 1 Τ 一 I I - Ding entropy, q field basin, 3-ethyl-1-pentene, 4_ methyl group - 1 pentene, 44 τ 1-1-pentene, 4 dimethyl-1-hexene, 4,4-methyl, a olefin, 4,4~, a-methyl-p-pentene, 4 ethyl-b-hexane, b-octene, diterpenoid, 3~undecene, tetradecene,

2254-10158-PF 200932476 卜十六碳烯、1-十八碳烯、卜二十碳烯等。又,於該等α — 烯烴成分,可以單獨i種或同時使用2種以上。該等之中單 獨使用乙烯最佳。 [[2]以通式(I)表示的環狀烯烴成分] 、說明在於可良好地使用於本發明之環狀烯烴成分與乙 烯等其他共聚合成分之加成聚合物,成為共聚合成分,以 通式(I)表示的環狀烯烴成分。 ❹ ❹ 在於通式(I)R1〜R12分別可為相同或不同、係選自由氣 原子、齒素原子以及由烴基組成之群。 的具體例,可舉例如氫原子··氟、氯、漠等齒素 原子;甲基、乙基、丙基、丁基等低級烧基等、該等可分 別相異,亦可部分地不同,又,亦可全部相同。 .素二的具體例’可舉例如氫原子;氟、氣、漠等 齒素原子’甲基、乙基、丙基'異丙基、丁基、 己基、硬腊基等的烷基;環己基等環烷 乙基苯基、異丙基苯基、蔡基甲本基、 香族烴基;爷其、〜、土等的取代或無取代芳 严基箄H 、丨基、於其他的貌基取代芳基之芳 说基等。料可以分別相異,亦可部分 之方 相同》 、或亦可全部 R與R或者R、R12一體化形成2價煙基 舉例如,亞乙基、亞丙基、異-體例’可 加。,或加互相形成環:等的亞燒基等。 亦可為多環,可為具有架橋的多環,亦可==可為單環 又亦可為該等環所組合之環。 〜雙層鍵結的環, 又’該等環亦可具有甲基等2254-10158-PF 200932476 hexadecene, 1-octadecene, and eicosene. Further, these α-olefin components may be used alone or in combination of two or more. It is best to use ethylene alone. [[2] a cyclic olefin component represented by the formula (I)] is an additive polymer which can be suitably used in the cyclic olefin component of the present invention and another copolymer component such as ethylene, and is a copolymerization component. A cyclic olefin component represented by the formula (I). ❹ 在于 In the formula (I), R1 to R12, respectively, may be the same or different and are selected from the group consisting of a gas atom, a dentate atom, and a hydrocarbon group. Specific examples thereof include a hydrogen atom, fluorine, chlorine, and a dentate atom; a lower alkyl group such as a methyl group, an ethyl group, a propyl group, or a butyl group; and the like may be different or partially different. And, they can all be the same. Specific examples of the second element include, for example, a hydrogen atom; an alkyl group such as fluorine, gas, or a dentate atom such as a methyl group, an ethyl group, a propyl group, an isopropyl group, a butyl group, a hexyl group, or a hard wax group; Hexyl and other cycloalkylethylphenyl, isopropylphenyl, benzylidene, aromatic hydrocarbon; substituted or unsubstituted aryl group 箄H, fluorenyl, etc. substituted by other morphologies The aryl group says base and so on. The materials may be different, or may be partially the same or may be all R and R or R, R12 integrated to form a divalent nicotine. For example, an ethylene group, a propylene group, or an iso-form may be added. , or add a ring to each other: a sub-base or the like. It can also be a multi-ring, which can be a multi-ring with a bridge, or == can be a single ring or a ring combined with the rings. ~ Double-bonded ring, and the rings can also have a methyl group, etc.

2254-10158-PF 12 200932476 取代基。 通式(I)所示的環狀烯烴成分的具體例,可舉二環 [2. 2. 1]庚-2-烯(慣用名:原冰片烯)、5-甲基-二環[2. 2. 1] 庚_2-稀、5,5_二甲基-二環[2.2.1]庚-2~~稀、5_乙基~~二環 [2. 2· 1]庚-2-稀、5 -丁基-二環[2· 2· 1]庚-2-稀、5-亞乙基 -二環[2· 2· 1]庚-2-烯、5-己基-二環[2· 2. 1 ]庚-2-烯、5-辛基-二環[2· 2.1]庚-2-稀、5 —h八烧基-二環[2. 2.1]庚 -2-烯、5-亞曱基-二環[2. 2. 1]庚-2-烯、5-乙烯基-二環 © [2. 2. 1]庚-2-烯、5-丙烯基-二環[2. 2. 1]庚-2-烯等2環環 狀烯烴; 三環[4.3.0.12’5]癸-3,7-二烯(慣用名:二環戊二 烯)、三環[4· 3. 0· I2’5]癸-3-烯;三環[4. 4· 0· I2’5]十一碳 -3, 7-二烯或三環[4. 4. 0. I2’5]十一碳-3, 8-二烯或者該等 的部分加氫物(或環戊二烯及環己烯的加成物)之三環 [4.4.0.I2’5]十一碳-3-烯;5-環戊基-二環[2.2.1]庚-2-稀、5 -環己基_二環[2.2.1]庚-2 -稀、5 -環己稀基-二環 w [2. 2. 1 ]庚-2-烯、5-苯基二環[2. 2· 1 ]庚-2-烯等的3環環狀 烯烴; 四環[4. 4· 0. I2’5. Γ1。]十二碳-3-烯(亦單稱為四環十 二碳烯)、8-曱基四環[4. 4. 0. I2,5. I7’1。]十二碳-3-烯、8-乙基四環[4. 4. 0. I2’5.厂’10]十二碳-3-烯、8-亞甲基四環 [4_4.0·12’5.Γ’1()]十二碳-3-烯、8-亞乙基四環 [4.4.0.12’5.17’1D]十二碳-3-烯、8-乙烯基四環 [4_ 4. 0. I2’5. Γ’111]十二,碳-3-烯、8-丙烯基-四環 2254-10158-PF = 13 200932476 [4.4.0.iu.r’u]十二碳_3_烯等的4環環狀稀烴;換段^ 環戊基-四環[“.Ο.12,5.17’1。]十二碳1埽、8-環己基-四 環[U.0.125·17,1。]十二碳-3~稀、8-環己烯基—四環 [4‘4‘i1 22 55 ’l71°]十m 8'笨基-環戊基-四環 四碳-U,u,13-四烯(亦稱為 ❹ ❹ 經基们;四環[8.4.l4,7.〇1,u.〇3.8]十五碳-5,10,12,14-四 稀(亦稱w’Mfm4a’5,1Q,1Ga_A^i);^ (6.6.1.m,14]-4-十六碳烯、五環 [6.5.1.1-.〇-.〇9,13]_4_ 十五 環 ^ 邱 、五環 [7.4.〇,〇ul3’6.lle,13]_4_ 十五碳埽七環 [8*7.0.12.9.14,7.lu’m-5-二十碳晞、七, 。12,广二十碳 - 烯的4聚物等的多環環狀烯烴。 A — ^該等環狀稀烴成分可以單獨,亦可調合2_0 [1]以碳數2〜_α_稀烴成分與[2]通式( 烯煙成分的聚合方法及所得聚合物的加氧方法,環狀 限定’可按照習知的方法進行。可為無規共聚合、:= 後段共聚合。 可為 又’關於使用的聚合觸媒亦並無特別限定 前習知的齊格勒·納塔系,複開環系、茂金屬系觸媒=先 觸媒以習知的方法得到。可良好地使用於本發 、的 ,烴及α-烯烴加成共聚物或其加氫物,最好使用茂金烯2254-10158-PF 12 200932476 Substituent. Specific examples of the cyclic olefin component represented by the formula (I) include bicyclo[2.2.1]hept-2-ene (common name: norbornene), 5-methyl-bicyclo[2] 2. 1] Geng_2-diluted, 5,5-dimethyl-bicyclo[2.2.1]heptane-2~~diluted, 5-ethyl-~~bicyclo[2. 2·1]heptane- 2-distilled, 5-butyl-bicyclo[2·2·1]hept-2-diene, 5-ethylidene-bicyclo[2·2·1]hept-2-ene, 5-hexyl-di Ring [2· 2. 1 ]hept-2-ene, 5-octyl-bicyclo[2·2.1]hept-2-ene, 5-h-octyl-bicyclo[2.2.1]hept-2- Alkene, 5-indenyl-bicyclo[2.2.1]hept-2-ene, 5-vinyl-bicyclo[2.2.1]hept-2-ene, 5-propenyl-di a 2-ring cyclic olefin such as a ring [2.2.1]hept-2-ene; a tricyclo[4.3.0.12'5]indole-3,7-diene (common name: dicyclopentadiene), a tricyclic ring [4. 3. 0· I2'5] indole-3-ene; tricyclo[4. 4· 0· I2'5] undecen-3, 7-diene or tricyclo[4. 4. 0. I2'5] undecane-3, 8-diene or a partial hydrogenation (or an adduct of cyclopentadiene and cyclohexene) of the tricyclic ring [4.4.0.I2'5] Monocarb-3-ene; 5-cyclopentyl-bicyclo[2.2.1]hept-2-diene, 5-cyclohexyl-bicyclo[2.2.1]heptane-2-dilute, 5-cyclohexyl - Second ring w [2. 2. 1] a 3-ring cyclic olefin such as hept-2-ene, 5-phenylbicyclo[2. 2·1]hept-2-ene; tetracyclic [4. 4· 0. I2'5. Γ1 . ]Dodeca-3-ene (also referred to simply as tetracyclododecarbene), 8-mercaptotetracyclo[4. 4. 0. I2, 5. I7'1. ]Dodeca-3-ene, 8-ethyltetracycline [4. 4. 0. I2'5. Plant '10] dodeca-3-ene, 8-methylenetetracycline [4_4.0· 12'5.Γ'1()]dodec-3-ene, 8-ethylenetetracyclo[4.4.0.12'5.17'1D]dodec-3-ene, 8-vinyltetracycline [4_ 4. 0. I2'5. Γ'111] Twelve, carbon-3-ene, 8-propenyl-tetracyclic 2254-10158-PF = 13 200932476 [4.4.0.iu.r'u] twelve carbon a 4-ring cyclic dilute hydrocarbon such as _3_ene; a group of cyclopentyl-tetracyclo[". Ο.12, 5.17'1.] twelve carbon 1 埽, 8-cyclohexyl-tetracyclo[U. 0.125·17,1.]12-carbon-3~dilute, 8-cyclohexenyl-tetracyclo[4'4'i1 22 55 'l71°] ten m 8' stupyl-cyclopentyl-tetracyclic four Carbon-U, u, 13-tetraene (also known as ❹ ❹ ❹; four rings [8.4.l4,7.〇1,u.〇3.8] fifteen carbon-5,10,12,14-four Rare (also known as w'Mfm4a'5,1Q,1Ga_A^i);^ (6.6.1.m,14]-4-hexadecene, pentacyclic [6.5.1.1-.〇-.〇9,13 ]_4_ fifteen rings ^ Qiu, Wuhuan [7.4. 〇, 〇ul3'6.lle, 13]_4_ fifteen carbon 埽 seven rings [8*7.0.12.9.14, 7.lu'm-5- twenty a polycyclic cyclic olefin such as a carbonium, seven, or twelve, a tetracene-ene tetramer, etc. A - ^ The cyclic dilute hydrocarbon component may be used alone or in combination with 2_0 [1] as a carbon number 2 to _α_dilute hydrocarbon component and [2] formula (method of polymerization of the olefin component and oxygenation method of the obtained polymer, ring-shaped ' can be carried out according to a conventional method. It can be a random copolymerization, : = a later stage copolymerization. It can also be a 'Zigler Nata system for the use of the polymerization catalyst, and there is no particular limitation on the former. Open-ring system, metallocene catalyst = first catalyst obtained by a known method. It can be suitably used in the present invention, hydrocarbon and α-olefin addition copolymer or hydrogenated product thereof, preferably using gold Alkene

2254-10158-PF 14 200932476 媒或齊格勒.納塔系觸媒製造。 複開環觸媒,可舉習知使用作為環烯烴的開環聚合用 觸媒的鉬或鎢系複開環觸媒(例如日本特開昭58 — 127728號 么報、同58-129013號公報等所記載)。又,使用複開環觸 媒所得之聚合物是無機載體負載的遷移金屬觸媒,將主鏈 的雙鍵鍵結的90%以上,侧鏈的芳香環中的碳—碳雙鍵鍵結 的98%以上加氫為佳。 [其他共聚合成分]2254-10158-PF 14 200932476 Media or Ziegler Natta is a catalyst manufacturer. For the reopening of the ring catalyst, it is known to use a molybdenum or tungsten-based reopening ring catalyst as a catalyst for ring-opening polymerization of a cyclic olefin (for example, JP-A-58-127728, JP-A-58-129013) Etc.). Further, the polymer obtained by using the reopening ring catalyst is an inorganic carrier-supported transition metal catalyst, and more than 90% of the double bond of the main chain is bonded, and the carbon-carbon double bond in the aromatic ring of the side chain is bonded. More than 98% hydrogenation is preferred. [other copolymerization ingredients]

可特別良好地使用於本發明之組成物之(a2)環狀烯烴 =α-烯烴加成共聚物,於上述的[〗]碳數2〜2〇的烯烴成 分及[2]通式(I)所示的環狀烯烴成分之外,在不損及本發 明的目的之範圍’可按照需要亦可含有其他的可共聚合之 不飽和單體成分。 可任意共聚合之不飽和單體,並無特別限定者,可舉 例如於i分子内包含2個以上的碳_碳雙鍵鍵結之烴系單體 等於1刀子内包含2個以上的碳—碳雙鍵鍵結之煙系單體的 具體例,可舉1 4- p -、膝 1 β ^ β 竿U己一烯、υ一辛二烯、2_甲基一^一己二 稀4-甲基-己二稀、5_甲基义^己二稀、6m 庚二稀、7-甲基—U—辛二烯等的鍵狀非共車厄二稀;環己二 稀、二環戊二歸 '甲基讀基節、乙烯基-2-原冰片埽、 5-亞乙基-2-原冰片婦、5_亞甲基2一原冰 -原冰片婦、6-氯甲…丙…-原冰片稀丙基 4’ 9, 5, 8-_ 亞甲基 _3a,4, 4a,5, 8, 8a,9, 9a_八羥, 茚等的環狀非絲二稀;2, 3 —二異.亞丙基〜5-原冰,片烯;2_The (a2) cyclic olefin = α-olefin addition copolymer which can be particularly preferably used in the composition of the present invention, the olefin component having a carbon number of 2 to 2 Å in the above [], and the formula (2) In addition to the cyclic olefin component shown, other copolymerizable unsaturated monomer components may be contained as needed in the range which does not impair the object of the present invention. The unsaturated monomer which can be arbitrarily copolymerized is not particularly limited, and for example, a hydrocarbon-based monomer having two or more carbon-carbon double bonds in the i molecule is equivalent to one or more carbons in one knives. - Specific examples of the carbon double bond-bonded flue monomer may be 1 4-p-, knee 1 β ^ β 竿 U hexene, υ-octadiene, 2-methyl-di-hexanene 4 -Methyl-hexamethylene dichloride, 5-methylexene dichloride, 6m heptane dilute, 7-methyl-U-octadiene, etc. Cyclopentanediolate 'methyl read base section, vinyl-2-original borneol, 5-ethylidene-2-original borneol, 5_methylene 2, raw ice-original borneol, 6-chloroform ...C...-original borneol propyl 4' 9, 5, 8-_ methylene _3a, 4, 4a, 5, 8, 8a, 9, 9a octa hydroxy, fluorene, etc. ; 2, 3 - diiso. propylene ~ 5 - raw ice, ene; 2_

2254-10168-PF 15 200932476 亞乙基3 -異亞丙基-5-原冰片烯;2 -丙稀基-2, 2-二環庚二 烯等。該等之中,以i’4—己二烯、辛二烯、及環狀非 共軛二烯、尤其以二環戊二烯、5 —亞乙基_2_原冰片烯、卜 乙烯基-2-原冰片烯、5-亞甲基-2-原冰片烯、1,4-己二烯、 1,6 -辛二稀為佳。 ❹ ❹ 環狀烯烴系樹脂之玻璃轉移溫度只要為8 01以上即 可,例如為8(TC〜180°C,以10(TC〜170°C為佳,以li〇t:〜16〇 C更佳。再者,破璃轉移温度,可藉由調整共聚合成分的 比例、分子量等而控制。用於本發明之環狀烯烴樹脂玻璃 轉移溫度(Tg),係根據JISK7121所記載的方法,採用以升 溫速度1 〇 /分的條件測定之值。 環狀烯烴系樹脂以數目平均分子量超過1〇〇〇〇之高分 子里環狀烯烴系樹脂為佳。更具體而言,環狀烯烴系樹脂 之數目平均分子量以15_〜彻_為佳,以2_(M〇〇_ 更佳,進一步以30000〜80000為佳。 〈低分子量環狀烯烴系樹脂〉 低刀子量環狀婦烴系樹脂,可例示於上述環狀稀煙系 樹脂之項所例示之環狀稀烴系樹脂。該等環狀稀烴系樹脂 2喜由相溶性等的觀點’使用與環狀稀煙系樹月旨相同系 統或者同種的樹脂為佳。 低刀子量環狀聚烯系樹脂為共聚物 (例如乙婦等的…類)的比例,可由全單二= ==選擇,惟從外觀特性等的方面,可為例如= 冥耳/以55〜95莫耳%左亡发社 、 為佳。知·別是,共聚合性單體為2254-10168-PF 15 200932476 Ethylene 3-isopropylidene-5-norbornene; 2-propenyl-2,2-dicycloheptadiene. Among these, i'4-hexadiene, octadiene, and cyclic non-conjugated dienes, especially dicyclopentadiene, 5-ethylidene-2-formerene, and vinyl -2-Ornirolene, 5-methylene-2-norbornene, 1,4-hexadiene, 1,6-octane dilute is preferred. ❹ 玻璃 The glass transition temperature of the cyclic olefin resin may be 801 or more, for example, 8 (TC to 180 ° C, preferably 10 (TC to 170 ° C, more preferably 〇 :: 〜16 〇 C Further, the glass transition temperature can be controlled by adjusting the ratio of the copolymerization component, the molecular weight, etc. The glass transition temperature (Tg) of the cyclic olefin resin used in the present invention is based on the method described in JIS K7121. The cyclic olefin resin is preferably a cyclic olefin resin having a number average molecular weight of more than 1 Å. More specifically, a cyclic olefin resin is used. The number average molecular weight is preferably 15_~che_, and 2_(M〇〇_ is more preferable, and further preferably 30,000 to 80,000. <Low molecular weight cyclic olefin resin> Low-knife amount of cyclic hydrocarbon resin, The cyclic rare hydrocarbon resin exemplified in the above-mentioned ring-shaped thin-smoke resin is used. The same is true from the viewpoint of compatibility and the like. Or the same kind of resin is preferred. The low knife amount of cyclic polyolefin resin is The ratio of the copolymer (for example, a class such as a woman) can be selected by the whole single ====, but in terms of appearance characteristics and the like, it can be, for example, = 耳耳/55 to 95 mol% left, It’s better. Know, don’t, the copolymerizable monomer is

2254-10158-PF 16 200932476 乙稀時,〔稀的比例,由外觀特性等的方面,可為例如6㈣ 莫耳%,以70~85莫耳%左右為佳。 低刀子量環狀烯烴系樹脂之玻璃轉移溫度,以7〇艺以 下為佳,以40t〜70t更佳。玻璃轉移溫度只要在7〇1以 下則低为子量環狀稀煙系樹脂,將會較通常的環狀稀煙 系樹腊先Μ,故在㈣成料,可緩㈣桿施於環狀稀 烴系樹脂之剪力。因此,可抑制凝膠狀物的產生而佳,只2254-10158-PF 16 200932476 When ethylene is thin, [thin ratio, depending on the appearance characteristics, etc., may be, for example, 6 (four) mole %, preferably about 70 to 85 mole %. The glass transition temperature of the low-knife amount cyclic olefin resin is preferably 7 Å or less, more preferably 40 t to 70 t. If the glass transition temperature is below 7〇1, it will be a sub-quantity ring-shaped thin-smoke resin, which will be more common than the normal ring-shaped flue-cured tree wax. Therefore, in the case of (4), the (four) rod can be applied to the ring. Shear force of dilute resin. Therefore, the generation of the gel can be suppressed, and only

要在40C以上’可以固體使用故高濃度染色配料化時容易 處理而佳。 低为子量環狀烯烴系樹脂之玻璃轉移溫度,較上述環 狀烯烴系樹脂之玻璃轉移溫度更低為佳。其差距以阶 ~100°c為佳,以20°c〜1001更佳。 、低分子量環狀埽烴系樹脂之數目平均分子量為1〇〇〇〇 以下。其數目平均分子量以5〇〇〜_〇為佳,以1〇〇〇~7〇〇〇 更佳,進一步以1500〜6000為佳。 述襄狀烯烴系樹脂及低分子量環狀烯烴系樹脂之數 目平句刀子里的差距並無特別被限定,以W〇為 佳,以 10000〜15〇〇〇〇f4,A t υ更佳進一步以200〇(Μ〇〇〇〇〇為佳, 以 30000〜80000最祛。μ .+、„ __ 上达%狀烯烴部樹脂與低分子量環狀 稀炫系樹脂之數目平於八« 十均刀子量差只要在1 000以上,由於抑It is easy to handle at a high concentration of 40 C or more. The glass transition temperature of the low-quantity cyclic olefin resin is preferably lower than the glass transition temperature of the above cyclic olefin resin. The difference is preferably in the order of ~100 °c, more preferably in the range of 20 ° c to 1001. The number average molecular weight of the low molecular weight cyclic terpene hydrocarbon resin is 1 Å or less. The number average molecular weight is preferably 5 〇〇 to _ ,, more preferably 1 〇〇〇 to 7 ,, and further preferably 1500 to 6,000. The difference between the number of the olefin-like olefin resin and the low-molecular-weight cyclic olefin resin is not particularly limited, and it is preferably W 〇 10000 〜 15 〇〇〇〇 f4, A t υ is further improved. 200 〇 (Μ〇〇〇〇〇 is better, 30,000~80000 祛. μ.+, „ __ The number of olefin-based resin and low-molecular-weight ring-shaped sleek resin is equal to eight « The difference in the amount of the knife is only 1 000 or more, because

制產生凝膠狀物的效果將繼、M 双果將變的顯者而佳,只要在200000以 下可使加工溫度差A交-Wr .»*· ρτι 在谷許軏圍内,並不會對成形時的加工 性帶來不良影響而佳。 [高濃度染色配料]The effect of producing a gel will be improved, and the M double fruit will become better. As long as it is below 200000, the processing temperature difference A will be -Wr.»*· ρτι in the valley, it will not It is preferable to have an adverse effect on the workability at the time of molding. [High concentration dyeing ingredients]

2254-10158-PF 17·2254-10158-PF 17·

❹ 200932476 本發明之特徵在於:將低分子量環狀烯烴系樹脂與環 狀烯烴系樹脂高濃度染色配料化而使用。藉由高濃度染色 配料化,可防止在射出成形時低分子量環狀烯烴系樹脂急 逮的熔融。因此,可提升樹脂咬入性,而可使成形材料順 =地移動。其結果,射出成形時每次的計量時間變短,可 提升射出成形品的生產性。 间濃度染色配料中的環狀烯烴系樹脂,以丨〇質量 質量%為佳。以2〇質量%〜9〇質量%更佳。高濃度染色配料中 的環狀烯烴系樹脂含量只要在上述範圍,低分子量環狀烯 烴系樹脂量與環狀烯烴系樹脂量同等以下,即可使高濃度 染色配料膠粒具有充分的韌性’粉的產生量少不容易引起 計量的問題而佳。 關於低刀子量環狀烯烴系樹脂以5質量%〜g〇質量%為 佳以10質量%〜80質:f %更佳。只要在5質量%以上,即有減 低凝膠之效果而佳,只要在9()質量%以下則低分子量環狀缚 =系樹脂之量與環狀稀煙系樹脂量為同等以了,即可使高 濃度染色配料膠粒具有充分的㈣,粉的產生量少不容: 引起計量的問題而佳。 南濃度染色配料之製作’係藉由將環狀烯烴系樹脂及 低分子量環狀稀煙系樹腊投人押出機,製作高濃度染色配 料為佳。押出機的種類並無特別限定。由於低分子量環狀 稀煙系樹脂之急速的溶融而難以在射出成形製作高濃度染 •於南濃度染色配料之製作 需要將環狀烯烴系樹脂及❹ 200932476 The present invention is characterized in that a low molecular weight cyclic olefin resin and a cyclic olefin resin are dyed and mixed at a high concentration. By the high concentration dyeing, it is possible to prevent the low molecular weight cyclic olefin resin from being rapidly melted during injection molding. Therefore, the resin biteability can be improved, and the molding material can be moved smoothly. As a result, the measurement time per injection is shortened, and the productivity of the injection molded article can be improved. The cyclic olefin resin in the intermediate concentration dyeing composition is preferably 丨〇 mass% by mass. It is more preferably 2% by mass to 9% by mass. When the content of the cyclic olefin resin in the high-concentration dyeing ingredient is within the above range, and the amount of the low molecular weight cyclic olefin resin is equal to or less than the amount of the cyclic olefin resin, the high-concentration dyeing rubber particles can have sufficient toughness. The small amount of production is not easy to cause the problem of measurement. The low-knife amount cyclic olefin-based resin is preferably 5% by mass to 5% by mass, more preferably 10% by mass to 80% by mass: f%. When the amount is 5% by mass or more, the effect of reducing the gel is good, and if it is 9% by mass or less, the amount of the low molecular weight cyclic ring-based resin is equal to the amount of the cyclic thin-smoke resin, that is, It can make the high-concentration dyeing rubber particles have sufficient (4), and the amount of powder generated is small: it is better to cause the measurement problem. It is preferable to produce a high-concentration dyeing compound by using a cyclic olefin-based resin and a low-molecular-weight ring-shaped tobacco tree to be extruded into a machine. The type of the extruder is not particularly limited. Due to the rapid melting of the low molecular weight cyclic thin-smoke resin, it is difficult to produce high-concentration dyeing by injection molding. • Preparation of dyeing ingredients in the south concentration requires the formation of a cyclic olefin resin and

2254-10158-PF 18 200932476 低分子量環狀烯烴系樹脂在押出機内,均勻混煉可塑化 於本發明,由於低分子量環狀㈣㈣脂會急速地溶融, 故料管溫度以18代〜340。〇為佳。以2〇〇t〜32(rc更佳。 又’螺桿的旋轉數以每分鐘5G轉〜每分鐘則轉為佳, 以每分鐘100轉〜每分鐘25〇Γριη轉更佳。關於押出量以 5kg/h卜200kg/hr為佳。以 1〇kg/h卜〗〇〇kg/hr更佳。 所得的高濃度染色配料之破璃轉移溫度以〗〇 〇 t以下 “…(^,。…。玻璃轉移温度只要在上述範圍 内,即可防立高濃度染色配料的急速熔融,可將為使射出 成形容易所需的低分子量環狀稀烴系樹赌,在射出成形時 順暢地輪送而佳。 [環狀烯烴系樹脂] _與^農度染色配料乾燥混合之環狀烯烴系樹月旨,可例 不含於高濃度染色配料之上述環狀烯烴系樹脂之說 示之相同者。 〇 肖高濃度染色配料乾燥混合之環狀烯烴系樹脂,可為 與含於高濃度染色配料之環狀稀烴系樹脂不同的樹脂惟 由相溶性等的觀點’使用同樣的樹脂為佳。 [射出成形] 本發明的特徵在於做射出成形。因此,將射出 成幾個步驟,說明使用上述高浪度染色配料為佳的理由二 射出成形,可分成材料投入步驟、可 保壓.冷卻步驟。 ’驟射出.2254-10158-PF 18 200932476 The low molecular weight cyclic olefin resin is uniformly kneaded in the extruder in the present invention. Since the low molecular weight cyclic (tetra) (tetra) grease is rapidly melted, the temperature of the tube is from 18 to 340. It is better. It is better to use 2〇〇t~32(rc. Also 'the number of rotations of the screw is 5G per minute~ every minute is better, and it is better to turn 100 rpm to 25 〇Γριη per minute. 5kg / h Bu 200kg / hr is better. 1 〇 kg / h 〗 〖 kg / hr better. The high concentration of dyeing ingredients obtained by the glass transfer temperature to 〗 〖t below "... (^, .... When the glass transition temperature is within the above range, the high-density dyeing ingredients can be rapidly melted, and the low-molecular-weight cyclic hydrocarbons which are required for easy injection molding can be smoothly transferred during injection molding. Preferably, the [cyclic olefin resin] is a cyclic olefin which is dry-mixed with the agricultural dyeing ingredient, and can be exemplified by the above-mentioned cyclic olefin resin which is not contained in the high-concentration dyeing ingredient. The cyclic olefin-based resin which is dried and mixed with a high-concentration dyeing ingredient may be a resin different from the cyclic rare-earth resin containing a high-concentration dyeing ingredient, and it is preferable to use the same resin from the viewpoint of compatibility and the like. [Injection Forming] The present invention is characterized in that injection molding is performed. Injection into several steps, using the above-described reasons of high waves dyeing ingredients preferably two injection molding, the material can be divided into steps, holding pressure cooling step. 'Step emitted.

&lt;材料投入步驟〉 2254-]〇l5S^PF 19 200932476 在於本發明之射出成形,其特徵在於乾燥混合。如果 不:乾燥混合,則由於出現在表面之低分子量環狀烯烴系 樹腊少’而無法有效地抑制凝膠狀物的產生。 雖然使用低分子量環狀烯烴系樹脂含量較多的環狀烯 烴系樹脂膠粒作為成形材料亦可使射出成形式變得容易。 但是,射出成形品中的低分子量環狀烯烴系樹脂含量變 多,則由於會降低拉張破斷伸度等的機械強度而不佳❶因 ❹&lt;Material input step&gt; 2254-] 〇l5S^PF 19 200932476 The injection molding of the present invention is characterized by dry mixing. If it is not: dry mixing, the generation of the gelatinous substance cannot be effectively suppressed due to the low molecular weight cyclic olefin wax which appears on the surface. The use of a cyclic olefin-based resin colloid having a high content of a low molecular weight cyclic olefin resin as a molding material can facilitate the formation of an injection. However, when the content of the low molecular weight cyclic olefin resin in the injection molded article is increased, the mechanical strength such as tensile elongation at break is lowered, which is not preferable.

此:有效地抑制凝膠狀物的產生、並且得到高品質的射出 成形品’需要做乾燥混合。 與高濃度染色配料乾燥混合之環狀烯烴系樹脂形狀, 並無特別限定,可為粉末但以膠粒為佳。 〈可塑化步驟&gt; 於可塑化步驟係將料斗所供給的環狀烯烴系樹脂、高 濃度染色配料等(成形材料)輸送·使之熔融,作成均質的 熔融體。 從料斗投入的環狀烯烴樹脂及高濃度染色配料等的成 形:料,#由螺桿的轉動從料斗側被輸送到噴嘴方向侧。 螺才于由料斗方側係以供給區(供給部)、壓縮區(壓縮部)、 計量區(計量部)所組成。 供給部,一般係以不會使樹脂膠粒熔融的溫度設定, 將樹脂膠粒從料斗向噴嘴方向輸送之作用。雖係以低溫進 =,作為溶融的準備階段以外部加熱器進行預熱。又,樹 月曰踢粒自於會被夾在旋轉的螺桿及料管間,對樹脂朦粒 加入摩擦力 而產生摩擦熱β玻璃轉移溫度低的低分子量This is effective in suppressing the generation of a gel and obtaining a high-quality injection molded article, which requires dry mixing. The shape of the cyclic olefin resin which is dry-mixed with the high-concentration dyeing ingredient is not particularly limited, and may be a powder, but it is preferably a rubber particle. <Plasticizing Step> In the plasticizing step, a cyclic olefin resin, a high-concentration dyeing ingredient, and the like (molding material) supplied from the hopper are conveyed and melted to form a homogeneous melt. The formation of the cyclic olefin resin and the high-concentration dyeing ingredients, etc., which are fed from the hopper, is transferred from the hopper side to the nozzle direction side by the rotation of the screw. The screw is composed of a supply zone (supply portion), a compression zone (compression section), and a metering zone (metering section) on the side of the hopper. The supply unit generally serves to transport the resin micelles from the hopper to the nozzle in a temperature setting in which the resin micelles are not melted. Although it is taken at a low temperature, it is preheated by an external heater as a preparation stage for melting. In addition, the tree scorpion kicking is sandwiched between the rotating screw and the material tube, and friction is added to the resin granules to generate frictional heat. The low molecular weight of the glass transition temperature is low.

W2254-10158-PF 20 200932476 環狀烯烴糸樹脂一般熔點多 柄八工θ s 孜低右使用含有多量如此之 低刀子置環狀烯烴系樹脂之 j細灸膠粒作為成形材料,則有因上 述預熱及摩擦熱而熔融之情形。 成形材料在此階段溶融,則會與螺桿共轉而益法有效 地輸送成形材料。又,即使&amp; …、 夕晚“ 包含很多低分子量環狀烯烴樹 月曰之膠粒並不完全地炼融情 會與環狀稀煙系樹脂勝 粒一起變成很大的團塊。該團塊 相較螺桿的溝較淺 ❹W2254-10158-PF 20 200932476 Cyclic olefin oxime resin generally has a melting point, multi-handle θ s 孜 右 low, using a fine moxibustion rubber particle containing a large amount of such a low-knife-set cyclic olefin resin as a molding material, Preheating and frictional heat and melting. When the forming material is melted at this stage, it is co-rotated with the screw to efficiently transport the forming material. Moreover, even if &amp; ..., evening "contains a lot of low-molecular-weight cyclic olefin tree, the rubber particles are not completely refining and become a large clump together with the ring-shaped thin resin." The block is shallower than the groove of the screw

則無法有效地將成形材料輸送。由於輸送無法順暢地進 X而將使每次的:量時間變長’而降低射出成形品的生 產性。又’由於輸送益法顺摇从 侧疋…、次m暢地進仃,因此每次 間差變大。因為計量時間的離散㈣對射^形 質 造成影響。 買 但是,為抑制凝膠狀物的產生,需要在、您融成形時, 使南濃度染色配料較環㈣烴系樹脂先熔化,減小施 狀烯烴系樹脂的剪力。為此需要低分子量環狀烯烴系樹浐 因此,如本發明,藉由使用包含環狀烯煙系樹腊及曰低 分子量環狀烯烴系樹脂之高漢度染色配料作為成形材料: 由於高濃度染色配料的玻璃轉移溫度及熔點會上升,而不 會在供應部熔i因此,只要將低分子量環狀燁煙= 與環狀烯烴㈣脂高濃度染色配料化使用,則可順暢^ 送低分子量環狀烯烴系樹脂。 3 為使成形材料的輸送順暢,高濃度染色配料之環 烴系樹脂為50質量%〜95質量%,以2〇質量%〜95質量%更佳。 又,為使輸送順暢,低分子量環狀烯烴系樹脂含量較The shaped material cannot be efficiently transported. Since the conveyance cannot be smoothly performed, the amount of time per time is increased, and the productivity of the injection molded article is lowered. In addition, because the transport benefit method is swung from the side 疋..., the second time is smooth, so the difference between each time becomes larger. Because the discrete (4) measurement time affects the shape of the radiation. However, in order to suppress the generation of gelatinous substances, it is necessary to melt the south concentration dyeing ingredients earlier than the ring (tetra) hydrocarbon resin to reduce the shearing force of the olefin-based resin. Low molecular weight cyclic olefinic taro is required for this purpose. Therefore, according to the present invention, a high-intensity dyeing formulation comprising a cyclic olefinic wax and a low molecular weight cyclic olefin resin is used as a forming material: The glass transition temperature and melting point of the dyeing ingredients will increase without melting in the supply part. Therefore, as long as the low molecular weight cyclic smog = high concentration dyeing of the cyclic olefin (tetra) is used, the low molecular weight can be smoothly sent. A cyclic olefin resin. 3 In order to smooth the conveyance of the molding material, the hydrocarbon resin of the high-concentration dyeing ingredient is 50% by mass to 95% by mass, more preferably 2% by mass to 95% by mass. Moreover, in order to smooth the transport, the content of the low molecular weight cyclic olefin resin is relatively

2254-10158-PF 21 200932476 少為佳’包含5質量%~80質量%之低分子量環狀烯烴系樹脂 為佳。以10質量60質量!更佳。 高濃度染色配料的玻璃轉移溫度以l〇〇〇c以下為佳。只 要是玻璃轉移溫度在i 00〇C以下,即可防止高濃度染色配料 在供應部熔出。因此可將包含低分子量環狀烯烴系樹脂的 高濃度染色配料順暢地輸送到壓縮區。高濃度染色配料更 佳的玻璃轉移溫度為5〇〇c〜1〇(rc,進一步以6〇()(::〜1〇〇它為 佳。 *&quot;、 0 壓縮。卩係隨著螺桿溝的深度將逐漸變淺。因此在壓縮 部,會對樹脂膠粒施加壓力。因此,在壓縮部會邊將樹脂 膠粒熔融,並且向前方(由料斗向喷嘴的方向)輸送。 會產生凝膠狀物的原因是在熔融時所受剪力。藉由包 含低分子量環狀烯烴系樹脂的高濃度染色配料較環狀烯烴 系樹脂先熔化,可緩和環狀烯烴系樹脂所受剪力。 於本發明,為使在於供應部的輸送順暢,使用包含環 狀烯烴系樹脂及低分子量環狀烯烴系樹脂的高濃度染色配 料。該高濃度染色配料雖較僅以低分子量環狀烯烴系樹脂 所構成之膠粒難溶化,但需使之成較環狀稀煙系樹脂膠粒 先熔化而緩和環㈣烴系樹脂所受剪力之高濃度染色配 料。 本發明的高濃度染色配料,為使包含低分子量環狀稀 煙系樹脂的高濃度染色配料較環狀烯烴系樹脂先炼出,而 包含5質量%〜8〇質量%极八 β 貞 低刀子I裱狀烯烴系樹脂為佳。以1 〇 質量%〜60質量%更佳。. 2254-10158-PF - 22 200932476 在此’高濃度染色配料會較先熔化是由於在高濃度染 色配料的表面存在有既定的低分子量環狀烯烴系樹脂。只 要低分子量環狀烯烴系樹脂之含量在於上述範圍内,先熔 化的低分子量環狀烯烴系樹脂可將環狀烯烴系樹脂所受的 剪力緩和。2254-10158-PF 21 200932476 It is preferable that it is a low molecular weight cyclic olefin resin containing 5 mass% to 80 mass%. With 10 quality and 60 quality! Better. The glass transition temperature of the high-concentration dyeing ingredient is preferably less than 10 °C. As long as the glass transition temperature is below i 00 〇C, high-concentration dyeing ingredients can be prevented from melting at the supply. Therefore, the high-concentration dyeing ingredient containing the low molecular weight cyclic olefin-based resin can be smoothly delivered to the compression zone. High-concentration dyeing ingredients have better glass transition temperature of 5〇〇c~1〇(rc, further 6〇()(::~1〇〇 it is better. *&quot;, 0 compression. Tethered with screw Since the depth of the groove is gradually shallower, pressure is applied to the resin colloid in the compression portion. Therefore, the resin colloid is melted in the compression portion and is conveyed forward (in the direction from the hopper to the nozzle). The reason for the gel is the shearing force at the time of melting. The high-concentration dyeing ingredient containing the low molecular weight cyclic olefin resin is melted first than the cyclic olefin resin, and the shearing force of the cyclic olefin resin can be alleviated. In the present invention, in order to smooth the transportation in the supply portion, a high-concentration dyeing ingredient containing a cyclic olefin resin and a low molecular weight cyclic olefin resin is used. The high-concentration dyeing ingredient is only a low molecular weight cyclic olefin resin. The formed colloidal particles are difficult to be melted, but it is required to be melted to form a high-concentration dyeing ingredient which is melted by the ring-shaped thin-smoke resin pellets to alleviate the shearing force of the ring (tetra) hydrocarbon-based resin. Make a low score The high-concentration dyeing ingredient of the ring-shaped thin-smoke resin is firstly refined than the cyclic olefin-based resin, and it is preferably contained in an amount of 5% by mass to 8% by mass of the extremely octa-β 贞 low knife I olefin-like resin. The mass % to 60% by mass is more preferable. 2254-10158-PF - 22 200932476 Here, the 'high-concentration dyeing ingredients will melt first because of the presence of a predetermined low molecular weight cyclic olefin resin on the surface of the high-concentration dyeing ingredient. When the content of the low molecular weight cyclic olefin resin is within the above range, the low molecular weight cyclic olefin resin which is first melted can alleviate the shearing force of the cyclic olefin resin.

❹ 又,由於低分子量環狀烯烴系樹脂亦為環狀烯烴系樹 脂’故若低分子量環狀烤烴系樹脂過多,則有因此時所受 剪力而產生凝膠狀物的危險性。因此,含於高濃度染色配 料之低刀子量%狀烯烴系樹脂的含量以上述範圍内為佳。 為降低低分子量環㈣烴系樹脂之含量,樹脂㈣的尺寸 以寬4襲〜1醜、長度5随〜lmffi,厚度4随〜為佳。 只要膠粒的大小在於上述範圍,即使使用少量的低分 子量環狀㈣樹赌,亦可提高低分子量環狀烯烴系樹脂出 現在膝粒表面的機率而佳。 為了普遍地緩和環狀烯烴系樹脂所受的剪力,使古濃 =配料,對與高濃度染色配料乾燥混合之環狀稀二 樹月曰10。質量部’使用5質量部,〇質量部為佳。以! 部〜100質量部更佳。 計量部,係使成形材料完全熔融,圖可塑化的均勾化, 錢=將此向前方輸送的作用。為得高品質的射出成形 因之或缺。可塑化會變的不均勻的原 意使用舍Γ成形材料開始㈣的溫度不同。於本發明’故 :配料射出:ΓΓΓ分子量環狀烯烴系樹脂高濃度染 出成形。因此,需要選擇可實現均句的可塑化的Further, since the low molecular weight cyclic olefin resin is also a cyclic olefin resin, if the low molecular weight cyclic baking hydrocarbon resin is too large, there is a risk that a gelling property will be generated due to shearing force. Therefore, the content of the low-knife amount of the olefin-based resin contained in the high-concentration dyeing composition is preferably in the above range. In order to reduce the content of the low molecular weight ring (tetra) hydrocarbon resin, the size of the resin (4) is as wide as 4 ug, the length 5 is ~lmffi, and the thickness 4 is preferably as follows. As long as the size of the colloidal particles is in the above range, even if a small amount of low molecular weight cyclic (four) tree bet is used, the probability of the low molecular weight cyclic olefin resin appearing on the surface of the knee surface can be improved. In order to generally alleviate the shearing force of the cyclic olefin-based resin, the sulphate = compounding, and the ring-shaped dilute tree 曰 10 which is dry-mixed with the high-concentration dyeing ingredients. The quality department 'uses 5 mass parts, and the mass part is preferable. To! Part ~ 100 quality parts is better. In the metering part, the molding material is completely melted, and the figure can be plasticized, and the money is transferred to the front. For high-quality injection molding, it is not enough. The plasticity becomes uneven and the original temperature is different from the starting point (4). In the present invention, the ingredient is injected: the ruthenium molecular weight cyclic olefin resin is dyed at a high concentration. Therefore, it is necessary to choose a plasticized one that can achieve a uniform sentence.

2254-10158-PF 23 200932476 成形材料。 為使可塑化均勻,用於 狀烯烴系樹脂含量以9 、 明之高濃度染色配料,環 系樹脂含量以5質量% φ θ 量公低刀子量環狀烯烴 配料,對與高濃度染色配 使該间濃度染色 質量部,使用5質量呷5〇暂:、’見合之環狀烯烴系樹脂100 量部更佳。 °質量部為佳。以丨。質量部質 為實現均勻的可塑化 ❹㈤高濃度染色配料及*㈣声::子量環狀烯烴系樹脂 浠烴系樹脂之破璃轉移染色配料乾燥混合之環狀 請。C更佳移如’⑽儒為佳。· 為實現均句的可塑化,需要 的壓縮比變大。另—士工A J屏燹淺使螺桿 形,需要—提升生產性而進行高循環成 影需要使计量部的溝變深使堡縮比變小。 縮比較/]、的上、 I 遣 Ή* Μ 匕較】的间循環成形時,為實現均勾的 螺桿長度及螺桿直;^n/rnMi ^ 萬要便 Q . . ^ ^a/D)變大。為均勻的可塑化及提升生 图在於本發H㈣终4之錢為佳,L 之範圍為佳。 3 在此,「屢縮比」,係指供應部1周期的容積 =期的容積之比。螺桿長度係指從料斗下到螺捍部尖料 〈射出.保壓·冷卻步驟〉 射出步驟係將熔融的樹脂由料管向模具 。射出速度及射出壓力係根據所使用之成形材料之較佳2254-10158-PF 23 200932476 Forming material. In order to make the plasticization uniform, the content of the olefin-based resin is dyed at a high concentration of 9 and a high concentration, and the content of the ring-based resin is 5% by mass φ θ, and the amount of the cyclic olefin is adjusted to a high concentration. For the inter-concentration dyeing quality portion, it is preferable to use a mass of 5 parts 呷5〇, and the amount of the cyclic olefin-based resin 100 is more preferable. ° Quality is preferred. Take 丨. Quality part quality To achieve uniform plasticization ❹ (5) High-concentration dyeing ingredients and * (4) Sound:: Sub-quantity cyclic olefin resin Resin-based resin-based glass transfer dyeing ingredients dry mixing ring. C is better to move as '(10) Confucianism is better. · In order to achieve the plasticization of the sentence, the required compression ratio becomes larger. In addition, the Shigong A J screen is shallow and screw-shaped, and it is necessary to improve the productivity and carry out high cycle formation. It is necessary to make the groove of the metering section deeper and the tonnage ratio becomes smaller. In the case of the intermediate cycle forming, the screw length and the screw straightness of the hook are compared; ^n/rnMi^ is always Q. . ^ ^a/D) Become bigger. For the uniform plasticization and promotion of the picture, the money of the end of the H (four) is better, and the range of L is better. 3 Here, the “recurring ratio” refers to the ratio of the volume of the supply unit for one cycle to the volume of the period. The screw length refers to the tip from the hopper to the screw tip. [Ejection. Pressure keeping and cooling step] The injection step is to transfer the molten resin from the tube to the mold. The injection speed and the injection pressure are preferably according to the molding material used.

2254-10M8-PF 24 200932476 的射出速度射出。 保壓步驟’係將熔融的成形材料射出後,由射出成形 裝置的料管側經由模具的澆口部對模穴内的熔融樹脂持續 施加壓力的步驟。隨著冷卻模穴内的樹脂體積會收縮,藉 由進行保壓可對模穴内補充熔融樹脂。因此,可抑制模穴 内的過剩的體積收縮。再者,藉由保壓澆口密封時間以上 的時間可保持一定的品質。 [實施例] 以下,舉出實施例更加詳細地說明本發明,本發明並 非受限於該等實施例者。 [材料] 與高濃度染色配料乾燥混合之環狀烯烴系樹脂(樹脂 A):Topas Advanced Polymers GmbH公司製、商品名 「TOPAS5013」,數目平均分子量40000’玻璃轉移溫度14〇 。。。 含於南濃度染色配料之環狀烯烴系樹脂(B1):2254-10M8-PF 24 200932476 The injection speed is emitted. The pressure holding step is a step of continuously applying pressure to the molten resin in the cavity through the gate portion of the mold from the side of the tube of the injection molding apparatus after the molten molding material is ejected. As the volume of the resin in the cooling cavity shrinks, the molten resin can be replenished in the cavity by holding pressure. Therefore, excessive volume shrinkage in the cavity can be suppressed. Furthermore, a certain quality can be maintained by sealing the gate for a time longer than the sealing time. [Examples] Hereinafter, the present invention will be described in more detail by way of examples, which should not be construed as limited. [Material] A cyclic olefin resin (Resin A) which is dry-mixed with a high-concentration dyeing ingredient: manufactured by Topas Advanced Polymers GmbH, trade name "TOPAS5013", and a number average molecular weight of 40,000 Å glass transition temperature of 14 Å. . . Cyclic olefin resin (B1) containing dyeing ingredients in the south concentration:

Advanced Polymers GmbH公司製、商品名「TOPAS5〇1〇」, 數目平均分子量30000,玻璃轉移溫度no 。 低分子量環狀烯烴系樹脂(B2):T〇pas Advanced Polymers GmbH公司製,商品名[T0PAS TM],數目平均分子 量4400,玻璃轉移溫度67°C。 [分子量的測定方法] 上述成形材料的數目平均分子量,係以如下條件測定。 (測定條件) 2254-10158-PF 25 200932476 裝置:Shodex SYSTEM-21CRI) 溶劑:甲苯(Nacalai HPLC等級)Manufactured by Advanced Polymers GmbH, the trade name "TOPAS5〇1〇", the number average molecular weight is 30,000, and the glass transition temperature is no. Low molecular weight cyclic olefin resin (B2): manufactured by T〇pas Advanced Polymers GmbH, trade name [T0PAS TM], number average molecular weight 4400, glass transition temperature 67 °C. [Method for Measuring Molecular Weight] The number average molecular weight of the above-mentioned molding material was measured under the following conditions. (Measurement conditions) 2254-10158-PF 25 200932476 Apparatus: Shodex SYSTEM-21CRI) Solvent: Toluene (Nacalai HPLC grade)

管柱:Polymer Laboratories公司製、MTXED-C(1 支) 流速:0. 8ml/分 溫度:40°C 試料濃度:0.2w/v %(預先用〇.2#m的薄膜過濾器過 遽) 注入量:10 0 # 1 標準試料:分子量 1〇9〇〇〇〇、706000、427000、1 90000、 96400、37900、18100、1 0200、5970、2630、1 050、500 的PS(0. lw/v%濃度的聚苯乙烯) 分析:評估換算PS的分子量 反覆測定之次數:2次 〈製作高濃度染色配料&gt; 以表卜2所示的配方將環狀烯烴系樹脂(A4B1)與低分 子量環狀稀烴系樹脂(B2)之混合物投入押出機(株式會社 曰本製鋼所製TEX30C) ’以料管溫度19〇 °c 、押出量 l〇kg/hr’螺桿旋轉數每分鐘15〇轉,製作長度2 5jnm,寬度 2. 5mm ’厚度2. 5mm之實施例卜1〇及比較例1、2之高濃度染 色配料。於實施例1雖可將高濃度染色配料押出,但是膠條 谷易折斷,一半成為長膠粒而不能說押出良好。 〈射出成形品之製作〉 以表1、2所示配方’將環狀烯烴系樹脂(A)的樹脂膠 粒、實施例或比較例的高濃度染色配料的樹脂膠粒(比較例.Column: Polymer Laboratories, MTXED-C (1) Flow rate: 0. 8ml / min Temperature: 40 ° C Sample concentration: 0.2w / v % (pre-measured with 薄膜.2#m membrane filter) Injection amount: 10 0 # 1 Standard sample: PS of molecular weights 1〇9〇〇〇〇, 706000, 427000, 190000, 96400, 37900, 18100, 1 0200, 5970, 2630, 1 050, 500 (0. lw/ v% concentration of polystyrene) Analysis: Evaluation of the molecular weight of the converted PS. The number of times of repeated measurement: 2 times <Preparation of high-concentration dyeing ingredients> The cyclic olefin resin (A4B1) and low molecular weight in the formulation shown in Table 2 The mixture of the cyclic dilute-based resin (B2) was put into the extruder (TEX30C manufactured by Sakamoto Steel Co., Ltd.) 'At the tube temperature 19 〇 ° C, the amount of extrusion l 〇 kg / hr' screw rotation number 15 rpm , a length of 2 5jnm, a width of 2. 5mm 'thickness of 2. 5mm of the example 1b and the high concentration dyeing ingredients of the comparative examples 1, 2. Although the high-concentration dyeing ingredients can be extruded in the first embodiment, the rubber strips are easily broken, and half of them become long rubber particles, and it cannot be said that the extrusion is good. <Preparation of injection-molded article> Resin colloidal particles of the cyclic olefin-based resin (A), resin granules of high-concentration dyeing ingredients of the examples or the comparative examples in the formulations shown in Tables 1 and 2 (Comparative Example).

2254-10158-PF 26 200932476 3僅以ί哀狀稀煙系樹鹿(A))作為樹脂肩姐4λ、丄 曰原科投入成形機(住友 重機械工業株式會社生產的SE75D)製 表作射出成形品。成形 條件,係使用7—角平板(膜繞口)作為模具,料管溫 度270 °C ’模具溫度lire ’射出逮度15Ws,保屋 30MPax3〇S,冷卻4Gs’計量5〇職,螺捍旋轉數每分鐘_ 轉,背景塵力15MPa,VP切換位置丨丨酿。 c ^ 所仔射出成形品為 長度70mm,寬度70mm,厚度2mm。 [評估1] ❹ ❹ 測定上述實施例以及比較例的射出成形品之成形時之 計量時間。敎次數為30次。計算計量時間的平均(獨, 及最長的計量時間與最短的計量時間 在將結果示於表 1 ° [評估2 ] 將實施例、比較例的射出成形品ig放進、的環己卜 用磁攪拌器以每分鐘500轉攪拌2小 &quot; 站 ★从 册射出成形品溶 解。之後’以目視評估溶液内的不溶物量。評估 不溶物之情形為5’不溶物少之情形為4,不小二 形為3 ’不溶物稍多之情來A 2 乂之It 等評估結果示於表^為不洛物多之情形為卜將該 [評估3] 除了將射出速度變更為4〇mm/s之 比較例同樣地得到射出#拟σ 上边實施例' 付主』射出成形品。以目視評估 其評估以盔噴霧椤勾盔一 . 出成形〇口, h夕之標記少之情形為◦,噴霧 標記夕之情形為X。將評估結果示於表b2254-10158-PF 26 200932476 3In the case of the sorrow of the smoky squirrel (A), it is produced as a resin shoulder sister 4λ, and the original injection molding machine (SE75D produced by Sumitomo Heavy Industries, Ltd.) Molded product. Forming conditions, using 7-angle flat plate (film wrap) as the mold, tube temperature 270 °C 'mold temperature lire' shot out of 15Ws, 30 megax3 〇S, cooling 4Gs' metering 5 捍, screw rotation The number is _ turn per minute, the background dust is 15 MPa, and the VP switching position is brewing. c ^ The molded article is 70mm in length, 70mm in width and 2mm in thickness. [Evaluation 1] ❹ 计量 The measurement time at the time of molding of the injection molded articles of the above Examples and Comparative Examples was measured. The number of times is 30 times. Calculate the average of the measurement time (individual, and the longest measurement time and the shortest measurement time. The results are shown in Table 1 ° [Evaluation 2] The injection molded article ig of the example and the comparative example is placed in the magnetic field. The stirrer is stirred at 500 rpm for 2 small &quot; station ★ from the book to spray the molded product to dissolve. Then 'visually evaluate the amount of insoluble matter in the solution. The situation of evaluating the insoluble matter is 5', the case of insoluble matter is 4, not small The dimorphism is 3' insoluble matter, and the evaluation result of A 2 乂 It is shown in the table ^ is the case of not more than the number of things is the same. [Evaluation 3] In addition to changing the injection speed to 4〇mm/s In the same manner as in the comparative example, the injection molded article was obtained by the example of the above-mentioned "paying main" injection. The evaluation was carried out by visual inspection. The helmet was sprayed with a helmet, and the shape of the mask was small. The case of the mark eve is X. The evaluation results are shown in the table b.

2254-10158-PF 27 200932476 [表1 ] 實施例1 實施例2 實施例3 實施例4 實施例5 實施例6 實施例7 實施例8 實施例9 實施例10 高濃度 染色配料 的組成 樹脂A (5013) 25 75 50 樹脂B1 (5010) 50 60 70 60 50 90 25 樹脂B2 (TM) 50 40 30 40 50 10 75 75 25 50 Tg(°C) 78 85 92 85 78 103 71 78 118 99 成形品的 組成 樹脂A 100 100 100 100 100 100 100 100 100 100 高濃度染 色配料 10 10 10 10 80 10 10 10 10 10 評估例 凝膠速率 4 4 4 4 4.5 3.5 4.5 4.5 3.5 4.5 噴霧標記 〇 〇 〇 〇 ◎ 〇 ◎ ◎ 〇 ◎ 計量時間 (AVG) 29.0 12.1 10.1 12.6 33.2 9,3 42.4 41.9 10,2 28.5 計量時間 (R) 23.3 3.6 1.9 2.3 26.2 1.2 25.7 28.6 1.5 22.5 *實施例4之高濃度染色配料有添加微量的滑劑2254-10158-PF 27 200932476 [Table 1] Example 1 Example 2 Example 3 Example 4 Example 5 Example 6 Example 7 Example 8 Example 9 Example 10 Composition of high-concentration dyeing ingredients Resin A ( 5013) 25 75 50 Resin B1 (5010) 50 60 70 60 50 90 25 Resin B2 (TM) 50 40 30 40 50 10 75 75 25 50 Tg (°C) 78 85 92 85 78 103 71 78 118 99 Composition Resin A 100 100 100 100 100 100 100 100 100 100 High Concentration Dyeing Ingredients 10 10 10 10 80 10 10 10 10 10 Evaluation Example Gel Rate 4 4 4 4 4.5 3.5 4.5 4.5 3.5 4.5 Spray Marking 〇〇〇〇 ◎ 〇 ◎ ◎ 〇 ◎ Measurement time (AVG) 29.0 12.1 10.1 12.6 33.2 9,3 42.4 41.9 10,2 28.5 Measurement time (R) 23.3 3.6 1.9 2.3 26.2 1.2 25.7 28.6 1.5 22.5 *High concentration dyeing of Example 4 Slip agent

[表2 ] 比較例1 比較例2 比較例3 高濃度染 色配料的 組成 樹脂A (5013) 樹脂B1 (5010) 100 樹脂B2 (TM) 100 TgCC) 67 110 成形品的 組成 樹脂A 100 100 100 高濃度染色配料 5 5 0 評估例 凝膠速率 5 1 1 喷霧標記 ◎ X X 計量時間 (AVG) &gt;60 8.8 8.6 計量時間(R) - 0.9 1.9 比較例1的計量時間平均超過6 0秒,最長的計量時間及 最短的計量時間之差無法測量。相對於此,實施例1〜1 0的 28[Table 2] Comparative Example 1 Comparative Example 2 Comparative Example 3 Composition of high-concentration dyeing ingredients Resin A (5013) Resin B1 (5010) 100 Resin B2 (TM) 100 TgCC) 67 110 Composition of molded article Resin A 100 100 100 High Concentration dyeing ingredients 5 5 0 Evaluation example Gel rate 5 1 1 Spray mark ◎ XX Metering time (AVG) &gt; 60 8.8 8.6 Metering time (R) - 0.9 1.9 The metering time of Comparative Example 1 averaged over 60 seconds, the longest The difference between the measurement time and the shortest measurement time cannot be measured. In contrast, Examples 1 to 10 of 28

2254-10158-PF 200932476 計量時間全部在6 0秒以内,且最長的計量時間及最短的計 量時間之差即使是最長者亦僅為28.6秒。因此,藉由將低 分子量環狀烯烴系樹脂與環狀烯烴樹脂高濃度染色配料化 使用,提升了射出成形品之生產性。特別是在於實施例 2〜4、6、9,平均的計量時間非常短,並且由於最長的計量 時間及最短的計量時間之差亦非常的短,可提升生產性的 同時’亦可得到射出成形品的品質穩定性的效果。2254-10158-PF 200932476 The measurement time is all within 60 seconds, and the difference between the longest measurement time and the shortest measurement time is only 28.6 seconds even if it is the longest. Therefore, by using a low-molecular-weight cyclic olefin-based resin and a cyclic olefin resin in a high-concentration dyeing, the productivity of the injection-molded article is improved. In particular, in Examples 2 to 4, 6, and 9, the average measurement time is very short, and since the difference between the longest measurement time and the shortest measurement time is also very short, the productivity can be improved and the injection molding can be obtained. The quality stability of the product.

在完全不使用低分子量環狀烯烴系樹脂之比較例2、 3確⑽到#常多的噴霧標記、不溶物(凝膠狀物)。相對於 此’實施m〜1()喷霧標記少’亦幾乎沒有確認料溶物(凝 /r物)目此’藉由使用包含低分子量環狀烯烴系樹脂的 高濃度染色配料,止射出成形品的外觀特性的降低。 【圖式簡單說明】 無 【主要元件符號說明】 無In Comparative Examples 2 and 3 in which the low molecular weight cyclic olefin-based resin was not used at all, the spray marks and insolubles (gels) of many (10) to # often were used. In contrast to the fact that the 'm~1() spray mark is small', there is almost no confirmation that the material (coag/r) is obtained by using a high-concentration dyeing ingredient containing a low molecular weight cyclic olefin resin. The appearance characteristics of the molded article are lowered. [Simple diagram description] None [Main component symbol description] None

2254-10158-PF 292254-10158-PF 29

Claims (1)

200932476 十、申請專利範圍: 1.種射出成形品的製造方法,使用環狀烯烴系樹埯 及數目平均分子量為1()_以下的低分子量環狀: 脂者, 尔銜 在將包含上述環狀烯烴系樹脂及上述低分子量環狀 烴系樹脂的高濃度染色配料及上述環狀稀煙系樹脂乾 合之步驟之後射出成形。 2·如申請專利範圍第1項所述的射出成形品的製造方 Ο法,其中上述高濃度染色配料係上述環狀稀煙系樹脂之含 量為20質f %至95質量%;上述低分子量環狀稀煙系樹脂之 含量為5質量%至8〇質量%之高濃度染色配料, 上述乾燥混合之步驟,係對上述環狀烯烴系樹脂ι〇〇 質量部,以5質量部至1〇〇質量部的高濃度染色配料混合。 3· —種高濃度染色配料,用於申請專利範圍第丨項所述 的射出成形品的製造方法者, 其中環狀烯烴系樹脂之含量為20質量%至95質量% ; ® 上述低分子量環狀烯烴系樹脂之含量為5質量%至質 量%。 4·如申請專利範圍第3項所述的高濃度染色配料,其中 上述低分子量環狀烯烴系樹脂之含量為1 〇質量%〜7〇質量%。 5_如申請專利範圍第3項所述的高濃度染色配料,其中 玻璃轉移溫度為100°C以下。 2254-10158-PF 30 200932476 七、指定代表圖: (一) 本案指定代表圖為:無 (二) 本代表圖之元件符號簡單說明:無200932476 X. Patent application scope: 1. A method for producing an injection molded article, which uses a cyclic olefin tree stalk and a low molecular weight ring having a number average molecular weight of 1 () or less: fat, which will contain the above ring The high-concentration dyeing ingredients of the olefin-based resin and the low-molecular-weight cyclic hydrocarbon-based resin and the step of dry-closing the above-mentioned cyclic thin-smoke-type resin are injection-molded. The method for producing an injection-molded article according to claim 1, wherein the high-concentration dyeing ingredient is a content of the cyclic thin-smoke resin of 20% by mass to 95% by mass; the above-mentioned low molecular weight The high-concentration dyeing ingredient having a content of the ring-shaped flue-cured resin of 5% by mass to 8% by mass, and the step of drying and mixing is the mass portion of the above-mentioned cyclic olefin-based resin ι〇〇, from 5 parts by mass to 1〇 The high-concentration dyeing ingredients of the 〇 mass section are mixed. A high-concentration dyeing ingredient for use in a method for producing an injection-molded article according to the above aspect of the invention, wherein the content of the cyclic olefin-based resin is from 20% by mass to 95% by mass; The content of the olefin-based resin is 5% by mass to 3% by mass. 4. The high-concentration dyeing composition according to claim 3, wherein the content of the low molecular weight cyclic olefin resin is from 1% by mass to 7% by mass. 5_ A high-concentration dyeing ingredient as described in claim 3, wherein the glass transition temperature is 100 ° C or less. 2254-10158-PF 30 200932476 VII. Designated representative map: (1) The representative representative of the case is: None (2) The symbol of the representative figure is simple: No 八、本案若有化學式時,請揭示最能顯示發明特徵的化學式: 無8. If there is a chemical formula in this case, please reveal the chemical formula that best shows the characteristics of the invention: 2254-10158-PF2254-10158-PF
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