TW593500B - Polyethylene resin composition for rotational molding and rotational molded product using the composition - Google Patents

Polyethylene resin composition for rotational molding and rotational molded product using the composition Download PDF

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Publication number
TW593500B
TW593500B TW89113425A TW89113425A TW593500B TW 593500 B TW593500 B TW 593500B TW 89113425 A TW89113425 A TW 89113425A TW 89113425 A TW89113425 A TW 89113425A TW 593500 B TW593500 B TW 593500B
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Taiwan
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ethylene
resin composition
polyethylene resin
copolymer
olefin copolymer
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TW89113425A
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Chinese (zh)
Inventor
Yoichiro Tsuji
Mutsuhiro Tanaka
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Mitsui Chemicals Inc
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Abstract

The polyethylene resin composition for rotational molding according to the invention is a composition comprising an ethylene-alpha-olefin copolymer (A) having a density of 0.880 to 0.930 g/cm<3> and MFR of 0.01 to 5 g/10 min and an ethylene homopolymer or an ethylene-alpha-olefin copolymer (B) having a density of 0.931 to 0.974 g/cm<3> and MFR of 0.5 to 20 g/10 min, wherein the weight ratio ((A)/(B)) of the component (A) to the component (B) is in the range of 10/90 to 50/50, and a blend consisting of these components (A) and (B) has a density of 0.920 to 0.960 g/cm<3> and MFR of 1 to 10 g/10 min. The component (A) is preferably a copolymer prepared by the use of a metallocene type olefin polymerization catalyst, and the component (B) is preferably a (co)polymer prepared by the use of a metallocene type or Ziegler type olefin polymerization catalyst. The rotational molded product of the invention comprises the polyethylene resin composition. According to the invention, a polyethylene resin composition for rotational molding which has excellent rotational moldability and is capable of producing rotational molded products superior to the conventional polyethylene rotational molded products in impact resistance and environmental stress crack resistance, and a rotational molded product using the composition can be provided.

Description

593500593500

五、發明説明( 部 智 慧 財 產 局 消 f 合 作 社 印 製 、、本發明涉及滾_的聚乙職脂組合物及用此組合物製 的,塑製品。更具體地說,本發明涉及使用於製備中空模塑件 ^複雜模餅續水_聚乙職齡合物,制是涉及用於 二塑的聚乙峨敝合物,由此組合物可製得具有優異耐衝擊 ,及耐環境應力開裂性(ESCR,environmental stress crack 咖对_)的冑品’本發明還涉及用此組合物製的滾塑製品。 (二6用滾塑法製造出各種製品如罐子、容器、日用品、 二二广園用了及至外用品。用於製這些製品的材料需要在機 ^又特別疋耐衝擊性和耐環境應力開裂性(ESCR)這些性 =面疋優異的。作爲符合這些需要的滾塑材料,聚 已被主要使用。 用艰乙稀納日經滾塑製得的物品在耐衝擊剛性及耐環境,力開裂財的-誠_是優異的,但在所有性能方面均優 :、的則很少。因此,在這魏能平衡方面好得多賴塑品是人 們所期待的。 -插权的日本公開特許公報194537/1997中,描述了 h袞脂’它包含乙稀—α—稀烴無規共聚物,其密度爲 (請先閱讀背面之注意事項再:本頁}V. Description of the invention (Printed by the Ministry of Intellectual Property, Co-operative Society, The present invention relates to a polyethylene glycol composition and a plastic product made from the composition. More specifically, the present invention relates to the use in preparing Hollow moldings ^ complex mold cake water renewal_Polyethene compound, which is a polyethylenimide compound used for second moulding, so that the composition can be made with excellent impact resistance and environmental stress cracking resistance ESCR (environmental stress crack coffee) _ The present invention also relates to rotomolded products made from this composition. (26) Various products such as jars, containers, daily necessities, The garden uses external products. The materials used to make these products require special mechanical properties such as impact resistance and environmental stress crack resistance (ESCR). These properties are excellent. As rotomolding materials that meet these needs, Poly has been mainly used. Articles made with Nissei Nikkei rotomolding are excellent in impact resistance, rigidity, and environmental resistance, and are capable of cracking money-sincerity_ is excellent, but it is excellent in all aspects of performance:, is very Less. Therefore, we can balance here The surface is much better, and plastic products are expected.-The Japanese Patent Publication No. 194537/1997, which is inserted, describes h-lipids, which contain ethylene-α-dilute hydrocarbon random copolymers with a density of ( Please read the notes on the back before: this page}

、1T, 1T

-! I I -1 · • —-1 I i · 本紙張尺度適用中國CNS ) A4規格( • n n . 593500-! I I -1 · • —-1 I i · This paper size applies to China CNS) A4 size (• n n. 593500

0立920-0· 9】5g/cm3,炼流指數(melt論乂)爲卜洲克/1〇分 鐘’ι分子里分佈(Mw/Mn)爲2-3,粒徑不大於30目。由此樹 月曰製成的滚塑製品特別在平衡耐衝擊性、剛性及耐環境應力開 裂性(ESCR)方面是優異的,使用方面沒有任何問題。 然而’其所能提供的滾塑製品在耐衝擊性及耐環境應力開 裂性(ESCR)方面優於用上述樹脂製的滾塑製品的聚乙烯樹 脂,現在仍是所期望的。 在這些情況下’本發明的發明人進行了認真的研+究以滿 足這些需求,而作爲其結果,他們發現,通過將下列樹脂組合 物進行滾塑而製得的聚乙烯滾塑製品,在耐衝擊性及耐環境應 力開裂性方面是優異的,此樹脂組合物含:(A)乙烯一 α-烯 烴共聚物,它含乙烯及具有3_2〇個碳原子的α—烯烴,密度 (ASTM D1505)爲 0.880-0· 930g/cm3,熔體流動速率(ASTM D1238 ’ 190 C ’負載2· 16Kg)爲〇. 〇卜5克/10分鐘,⑻含 經濟部智慧財產局員工消費合作社印製 乙卸的乙烯均水物’或含乙稀及具有3—2〇個碳原子的α—稀烴 的共承物。其岔度爲〇·93ΐ-〇.974g/cm3,溶體流動速率爲 〇.5-20克/1〇分鐘,其中(A) / (B)重量比處於特定範圍, 而包含乙烯—烯烴共聚物(A)及乙烯均聚物或乙烯— 烯烴共聚物(Β)的掺混物的密度爲〇·92〇—0 960g/cm3,熔體 流動速率爲1-10克/10分鐘。基於這一發現完成了本發明。 發明目的 6 、發明説明( 物,η月^個目的疋提供—種滾塑用的聚乙烯樹脂組合 製的滾 耐衝擊性和耐環境應力開裂性(_ 通纽賴品的滾塑製品,並提供使耻組合物: 發明相n 根據本發明的滾塑物㈣聚乙烯樹脂組合物是一種樹脂 組合物,它包含: (A) 3有乙烯及γ 3-20個碳原子的α—烯烴的乙稀一 α — 烯烴共聚物,其密度(ASTM D15Q5)爲G. __Q.謂g/cm3,炫 體流動速率(MFR) (ASTM D1238,190〇C ,負載:2.16Kg)爲 〇· 01-5克/1〇分鐘,及 (B) 含有乙烯的乙烯均聚物或含有乙烯及帶3—2〇個碳原 經濟部智慧財產局員工消費合作社印製 子的1^—烯烴的乙烯一 烯烴共聚物,其密度(ASTM D1505) 爲 〇·931-(H74g/cin3,熔體流動速率(MFR,melt flow rate) (ASTMD1238,190°C,負載:2· 16Kg)爲 〇· 5-20 克/10 分鐘, 其中,· 乙烯〜α-烯烴共聚物(A)與乙烯均聚物或乙烯一 α一烯 烴共聚物(Β)的重量比〔(A) / (Β)〕爲10/90-50/50,及 由乙烯〜α-烯烴共聚物(Α)與乙烯均聚物或乙烯一 α- 本紙張尺度適用中國國^準(€奶)八4規格(210、乂297公釐) ^3500 A7 B7 經濟部智慧財產局員工消費合作社印製 五、發明説明() 烯烴共聚物(B)組成的摻混物的密度(ASTM D1505 )爲 ^•92〇〜〇.960g/cm3,熔體流動速率(MFR) (ASTM D1238,19〇 °C,負载:2· 16Kg)爲H0克/1〇分鐘。 根據本發、明的用於滾塑的聚乙烯樹脂組合物可以採用下 列四個具體方案,這些具體方案基於在製造乙烯一α—烯烴共 命物(Α)、乙烯均聚物(Β)及乙烯烯烴共聚物(Β)時 所用烯垣聚合反應催化劑的類型來劃分。 (1) 一種樹脂組合物,其中乙烯—α—烯烴共聚物(Α)、 乙烯均聚物(Β)及乙烯一 α—烯烴共聚物(Β)中的每一個均 是用二茂金屬型(metallocene type)烯烴聚合反應催化劑製備 的(共)聚合物; (2) —種樹脂組合物,其中乙烯一烯烴共聚物 是用二茂金屬型烯烴聚合反應催化劑製的共聚合物,而乙烯均 聚物(B)及乙烯一α〜稀烴共聚物(β)是用齊格勒型(ziegler type)烯烴聚合反應催化劑製備的; (3) —種樹脂組合物,其中乙烯一 α—烯烴共聚物(A)、 乙炸均?物(B)及乙歸—α—稀烴共聚物(B)是用齊格勒型 烯烴聚合反應催化劑製備的;及 請 先 閎 讀 背 意 事 項 再0 920-0 · 9] 5g / cm3, the refining flow index (melt theory) is Bu Zhou Ke / 10 minutes' molecular distribution (Mw / Mn) is 2-3, the particle size is not greater than 30 mesh. The rotomolded products made from this tree are particularly excellent in balancing impact resistance, rigidity, and environmental stress crack resistance (ESCR), and there is no problem in terms of use. However, the rotomolded products it can provide are superior to polyethylene resins made of rotomolded products made of the above resins in terms of impact resistance and environmental stress cracking resistance (ESCR), and are still desired. Under these circumstances, 'the inventors of the present invention have conducted earnest research + research to meet these needs, and as a result, they have found that polyethylene rotomolded articles made by rotomolding the following resin compositions are It is excellent in impact resistance and resistance to environmental stress cracking. This resin composition contains: (A) ethylene-α-olefin copolymer, which contains ethylene and an α-olefin having 3 to 20 carbon atoms, and the density (ASTM D1505 ) Is 0.880-0 · 930g / cm3, and the melt flow rate (ASTM D1238 '190 C' load 2.16Kg) is 〇. 5 g / 10 minutes, including printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs Unloaded ethylene homogenates' or co-products of ethylene and alpha-dilute hydrocarbons with 3-20 carbon atoms. Its bifurcation degree is 0.93 to 0.9974 g / cm3, and the solution flow rate is 0.5 to 20 g / 10 minutes, in which the (A) / (B) weight ratio is in a specific range, and the ethylene-olefin copolymerization is included. The density of the blend of the polymer (A) and the ethylene homopolymer or the ethylene-olefin copolymer (B) is 0.992 to 960 g / cm3, and the melt flow rate is 1 to 10 g / 10 minutes. The present invention has been completed based on this finding. OBJECTS OF THE INVENTION 6. DESCRIPTION OF THE INVENTION (Objectives, η months ^ objectives)-to provide a kind of rotational impact resistance and environmental stress crack resistance made of a combination of polyethylene resins for rotational molding Provide a stigma composition: Inventive phase n A rotomolded product according to the present invention. A polyethylene resin composition is a resin composition comprising: (A) 3 α-olefins having ethylene and γ 3-20 carbon atoms. Ethylene-α-olefin copolymer, its density (ASTM D15Q5) is G. __Q. It is g / cm3, and the body flow rate (MFR) (ASTM D1238, 190 ° C, load: 2.16Kg) is 0.01-1. 5 g / 10 minutes, and (B) ethylene homopolymer containing ethylene or ethylene olefin containing 1 ^ -olefin printed by the consumer cooperative of employees of the Intellectual Property Bureau of the Intellectual Property Bureau of the Ministry of Economic Affairs with 3 to 20 carbon atoms Copolymer whose density (ASTM D1505) is 0.931- (H74g / cin3, melt flow rate (MFR) (ASTMD1238, 190 ° C, load: 2.16Kg) is 0.5-20 g / 10 minutes, where: · Weight of ethylene ~ α-olefin copolymer (A) and ethylene homopolymer or ethylene-α-olefin copolymer (B) The ratio [(A) / (Β)] is 10 / 90-50 / 50, and the paper is composed of ethylene ~ α-olefin copolymer (A) and ethylene homopolymer or ethylene-α- € milk) 8 specifications (210, 乂 297 mm) ^ 3500 A7 B7 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. Description of the invention () Density of the blend consisting of olefin copolymer (B) (ASTM D1505 ) Is ^ • 92〇 ~ .960g / cm3, and the melt flow rate (MFR) (ASTM D1238, 19 ° C, load: 2.16Kg) is H0 g / 10 minutes. According to the application of the present invention, Ming The following four specific schemes can be adopted for the rotomolded polyethylene resin composition. These specific schemes are based on the production of ethylene-α-olefin co-products (A), ethylene homopolymers (B), and ethylene olefin copolymers (B). (1) A resin composition in which an ethylene-α-olefin copolymer (A), an ethylene homopolymer (B), and an ethylene-α-olefin copolymer (B) are used. Each of them is (co) polymerized using a metallocene type olefin polymerization catalyst (2) A resin composition in which an ethylene-olefin copolymer is a copolymer made using a diocene metallocene-type olefin polymerization catalyst, and an ethylene homopolymer (B) and an ethylene-α ~ dilute hydrocarbon copolymer ( β) is prepared using a ziegler type olefin polymerization catalyst; (3) a resin composition in which an ethylene-α-olefin copolymer (A), an ethylene homopolymer (B), and an ethyl alcohol The homing-α-dilute hydrocarbon copolymer (B) is prepared using a Ziegler-type olefin polymerization catalyst;

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本紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐 (4)—種樹脂組合物,立中 是用齊袼勒㈣烴聚合反應催烴共聚物⑴ 化劑製備的。 )ϋ金屬型烯烴聚合反應催 和且合物⑴—⑷中,優選的是樹脂組合物⑴ 劑制備^ 每—種含有用二茂金屬型驗聚合反應催化 =:ί;Γα—烯烴共聚物⑷,及用齊格勒型烯烴聚合 4士^,二1衣備的乙細均聚物和乙稀—α,煙共聚物⑻。 二二3有用二茂金屬型烯烴聚合反應催化劑製備的乙稀- ’/ά物(Α)’齊格勒型烯烴聚合反應催化劑製備 勺乙細均聚物或乙稀—α_稀烴共聚物⑻的組合物是優越的。 根據本發明的滾塑製品含有上述用於滾塑的聚乙烯樹脂 組合物。 根據本發明的滾塑用的聚乙烯樹脂組合物及用此组合物 製的滾塑製品詳述如下。 根據本發明的滾塑用的聚乙烯樹脂組合物含有乙烯一 α -烯烴共聚物(Α),及其密度不同於共聚物(Α)的乙烯均聚物 或乙烯~α-烯烴共聚物(β),當此樹脂組合物由乙稀一α —This paper size is in accordance with Chinese National Standard (CNS) A4 specification (210X297 mm (4) —a resin composition, which is prepared using a hydrocarbon copolymerization catalyst for the polymerization of zilerene㈣ hydrocarbons.) ΫMetal type Among the olefin polymerization catalysts and compounds ⑷-⑷, it is preferable to prepare resin compositions 剂 each of which contains a metallocene-type polymerization polymerization catalyst =: Γ; Γα-olefin copolymer ⑷, and a combination of The Greer-type olefin was polymerized 4 ^, 2 fine homopolymers and ethylene-α, smoke copolymer ⑻. 223 Preparation of Ethylene Diene with a Metallocene-type Olefin Polymerization Catalyst-'/ ά 物 (Α)' Ziegler-type olefin polymerization catalyst for preparing thin homopolymer or ethylene-α_dilute hydrocarbon copolymer The rhenium composition is superior. The rotomolded article according to the present invention contains the above-mentioned polyethylene resin composition for rotomolding. The polyethylene resin composition for rotomolding according to the present invention and the rotomolded article made from the composition are described in detail below. The polyethylene resin composition for rotomolding according to the present invention contains an ethylene-α-olefin copolymer (A) and an ethylene homopolymer or an ethylene-α-olefin copolymer (β) having a density different from that of the copolymer (A). ), When this resin composition consists of ethylene-α-

593500 經濟部智慧財產局員工消費合作社印製 五、發明説明() 烯烴共聚物(A)與乙烯均聚物或乙烯1_稀煙q物⑻ 組成時,此樹脂組合物的密度和熔體_速率處在特定範圍。 乙烯...二^-趣座共聚物(n 用於本發明的乙稀—α—_共聚物⑷是乙稀和3一20 個石炭原子的α-烯烴的共聚物,密度(職_5)爲 80 0.930g/cm,優逑爲 0.885-0.925 g/cm3,更優選爲 ⑴890 〇· 920 g/cm ’其溶體流動速率(職)(AsT請238,190 c ’負載2· 16Kg)爲0· G1-5克/1◦分鐘,優選爲〇· 〇5_4· 5克 /10分鐘,更優選爲〇· 1-4· 0克/1〇分鐘。 3-20個碳原子的α-烯烴實例包括丙烯,丨_丁烯,卜戊烯, 2甲基-1-丁烯,3一曱基+ 丁烯,卜己烯。3一甲基一卜戊烯, 4甲基-1-戊稀,3,3-二曱基-1—丁烯,1 一庚烯,甲基己烯, —甲基-1-戊烯,三曱基一 1 一丁烯,乙基一丨―戊烯,卜辛烯,曱 基一 1-戊烯,二甲基—丨—己烯,三甲基—丨—戊烯,乙基一丨一己烯, 曱基乙基-1—戊烯,二乙基—丨―丁烯,丙基—丨―戊烯,丨―癸烯, 曱基一卜壬烯,二曱基-1-辛烯,三曱基-1-庚烯。乙基-1-辛烯, 甲基乙基-1-庚烯,二乙基—1—己烯,丨-十二碳烯,丨_十六碳烯。 這些α-烯烴可單獨用,或者兩種或多種合用。 10 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) —---- 請 先 閱 背, 面 之 注· 意 事 項593500 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. Description of the invention () When the olefin copolymer (A) is composed of ethylene homopolymer or ethylene 1_ thin smoke q q, the density and melt of this resin composition _ The speed is in a specific range. Ethylene ... Di-copolymer (n The ethylene-α-_ copolymer used in the present invention is a copolymer of ethylene and an alpha-olefin of 3 to 20 carbon atoms. ) Is 80 0.930 g / cm, and the optimal value is 0.885-0.925 g / cm3, more preferably 890,920 g / cm 'its solution flow rate (position) (AsT, please 238,190 c' load 2.16Kg) 0 · G1-5 g / 1 ◦min, preferably 0.05-4.5 g / 10min, more preferably 0-1.4.0 g / 10 min. Α- of 3-20 carbon atoms Examples of olefins include propylene, butene, pentene, 2-methyl-1-butene, 3-monomethyl + butene, and hexene. 3-monomethyl-pentene, 4-methyl-1- Pentylene, 3,3-Difluorenyl-1-butene, 1-heptene, methylhexene, —methyl-1-pentene, trimethyl-1-butene, ethyl-1-pentene Ene, buxene, fluorenyl-1-pentene, dimethyl- 丨 -hexene, trimethyl- 丨 -pentene, ethyl- 丨 hexene, fluorenylethyl-1-pentene, di Ethyl--butene, propyl--pentene, decene, fluorenyl-bronone, difluorenyl-1-octene, trimethylen-1-heptene. Ethyl -1-octene, methylethyl-1-heptene, diethyl-1-hexene, dodecene, hexadecene. These α-olefins can be used alone, or two kinds Or multiple combinations. 10 This paper size is applicable to China National Standard (CNS) Α4 specification (210 × 297 mm) —---- Please read the back first, the notes and notes

訂 線 赞明説明( +=優=::,聚_是乙稀 乙—叫峨物物物, -、有上述性施的乙稀— ::==r,合反細:=:二: 共聚而ίΓ ,將乙烯與㈣麵原子的樣 ^舞均聚物或乙嫌一 林=中使用的乙稀均聚物或乙稀—α,烴共聚物 =)’疋僅含乙烯的聚合物,或乙婦與3_2Q個碳原子的ι ㈣的共聚物,其密度(ASTM _5)爲Q. 931M). 974_3, 優選為 G. 935-G. 970 g/em3,更優選爲 ο. 938-G. 968 g/cm3 ,溶 體流動速率(MFR) (ASTM D1238,190°C,負載:2 16Kg) 2 0. 5-20克/l〇分鐘,優選爲丨.〇_19克/1〇分鐘,更優選爲A—= 克/10分鐘。 · 3-20個碳原子的α _稀烴實例包括與用於構成上述乙稀— α-稀垣共聚物(a)的3-20個碳原子的α_烯烴相同的以一稀 。3-20個碳原子的α-烯烴可以單獨使用,或者兩種或多種 593500 A7 五 、發明説明( B7 優: :選用於本發明中的乙稀—『烯 丁烯共聚物,乙稀+鱗共聚物 3=^乙~+ ―4—甲基+戊稀共聚物或乙朴辛稀共聚物、济乙烯(B) 刺料紅歸化劑的存 -烯烴共聚而The description of the line description (+ = You = ::, poly_ is a diethyl ether—named as ewuwuwu,-, a diethyl compound with the above-mentioned properties— :: == r, combined anti-refinement: =: two: Copolymerization and ΓΓ, the ethylene homopolymer or homopolymer or ethylene homopolymer = ethylene homopolymer or ethylene-α, hydrocarbon copolymer =) '疋 polymer containing only ethylene 938-, or a copolymer of Otome with 3_2Q carbon atoms, its density (ASTM _5) is Q. 931M). 974_3, preferably G. 935-G. 970 g / em3, more preferably ο. 938- G. 968 g / cm3, solution flow rate (MFR) (ASTM D1238, 190 ° C, load: 2 16Kg) 2 0.5-20 g / lOmin, preferably 丨 .19 g / l0 Minutes, more preferably A— = grams / 10 minutes. Examples of the α_lean hydrocarbons of 3 to 20 carbon atoms include the same ones as the α_olefins of 3 to 20 carbon atoms used to constitute the aforementioned ethylene-α-thin copolymer (a). Alpha olefins of 3-20 carbon atoms can be used alone, or two or more of 593500 A7 V. Description of the invention (B7 Excellent:: Ethylene selected for use in the present invention-"butene copolymer, ethylene + scale Copolymer 3 = ^ ethyl ~ + ― 4-methyl + pentylene copolymer or ethene copolymer, ethylene (B) resin red-naturalizing agent storage-olefin copolymerization

當使用以二茂金屬型稀烴聚合反應催化劑而 -烯烴共聚物作爲本發明的 製取的乙稀 乙烯—α—稀烴共聚物(Α)時,·訂 可以使用以二茂金屬賴烴聚合反應催化 聚物或乙烯一a—、擒柄丘〜Q砰, 料取二Λ 作爲乙烯均聚物或乙烯…歸 過用齊格勒型聚合反應催化劑而製得稀a 戈乙烯—a—烯烴共聚物可用作乙烯均聚物或乙 烯一烯烴共聚物(B)。 當使用以齊格勒型烯烴聚合反應催化劑而製取的乙烯— α、、〜、*物作爲本發嘱乙烯1-烯烴共聚物⑴時, ,使用以齊格勒型烯烴聚合反應催化劑而製取的乙烯均聚物 ’乙烯烯烴共聚物作爲乙稀均聚物或乙烯- α-烯烴共 聚物(Β)。 〃 劑而製得的乙烯均 12 本紙張尺度適用中國國家標準(CNS ) Μ規格(:獻挪公董 593500 A7 B7 五、發明説明( —在上述情況中,通過用二茂金屬輯烴聚合反應催化劑而 衣得的乙婦α-烯烴共聚物(a)與通過使用齊格勒型烯烴聚 合反應催化劑而製得的乙烯均聚物(組分⑻)的混合物是優 選的 請 先 閱 讀 背 經濟部智慧財產局員工消費合作社印製 里聚乙烯榭脂組会物 根據本發明的用於滾塑的聚乙烯樹脂組合物包含乙烯一 α-烯烴共聚物(A)及乙烯均聚物或乙烯—烯烴共聚物⑻。 在此樹脂組合物中,乙烯—烯烴共聚物(Α)及乙烯均 聚物或乙烯一α~烯烴共聚物(β)的重量比〔(a) / (Β)〕爲1〇/90—50/50,優選爲 15/85-45/55,更優選爲 20/80-40/60。 至於根據本發明的用於滾塑的聚乙烯樹脂組合物,由乙烯 一 a-烯烴共聚物(Α)與乙烯均聚物或乙烯—α—烯烴共聚物 (Β)組成的摻混物的密度(ASTMD15〇5)爲 〇· 92〇—〇. 96〇g/cm3, 優選爲 0· 922-0· 958g/cm3,更優選爲 0· 925-0· 955g/cm3,特別 優選爲0.930-0.955g/cm3,而熔體流動速率(MFR) (ASTM D1238,190°C,負載:2· 16Kg)爲 1-10 克/10 分鐘,優選爲 1· 5-9克/10分鐘’更優選爲2· 〇—8克/10分鐘。當此樹脂組合 之 注, 項·When using a metallocene-type dilute hydrocarbon polymerization catalyst and an olefin copolymer as the ethylene-α-dilute hydrocarbon copolymer (A) prepared in the present invention, it is possible to use dimetallocene lysene polymerization Reaction catalytic polymer or ethylene-a—, shovel Qiu ~ Q bang, take two Λ as ethylene homopolymer or ethylene ... and use the Ziegler-type polymerization catalyst to prepare dilute agoethylene-a-olefin The copolymer can be used as an ethylene homopolymer or an ethylene-olefin copolymer (B). When using ethylene-α ,, ~, * produced by using a Ziegler-type olefin polymerization catalyst as the ethylene 1-olefin copolymer of the present invention, it is prepared by using a Ziegler-type olefin polymerization catalyst. The ethylene homopolymer 'ethylene olefin copolymer was taken as the ethylene homopolymer or the ethylene-α-olefin copolymer (B). Ethylene produced by tinctures are all 12 paper sizes applicable to Chinese National Standards (CNS) M specifications (Xianguo Gongdong 593500 A7 B7 V. Description of the invention (-In the above case, the use of metallocene polymerization polymerization The catalyst is a mixture of ethylenic α-olefin copolymer (a) and an ethylene homopolymer (component IX) prepared by using a Ziegler-type olefin polymerization catalyst. Please read the Ministry of Economy first. Intellectual Property Bureau Employees' Consumer Cooperatives Printed Polyethylene Compounds The polyethylene resin composition for rotomolding according to the present invention contains ethylene-α-olefin copolymer (A) and ethylene homopolymer or ethylene-olefin Copolymer ⑻. In this resin composition, the weight ratio [(a) / (B)] of the ethylene-olefin copolymer (A) and the ethylene homopolymer or the ethylene-α to olefin copolymer (β) is 1%. / 90-50 / 50, preferably 15 / 85-45 / 55, and more preferably 20 / 80-40 / 60. As for the polyethylene resin composition for rotomolding according to the present invention, ethylene-a-olefin Copolymer (Α) and ethylene homopolymer or ethylene-α-olefin copolymer (B) The resulting blend has a density (ASTMD 1505) of 0.992-0.960 g / cm3, preferably 0.922-0. 958 g / cm3, and more preferably 0.925-0. 955 g / cm3. , Particularly preferably 0.930-0.955g / cm3, and the melt flow rate (MFR) (ASTM D1238, 190 ° C, load: 2.16Kg) is 1-10 g / 10 minutes, preferably 1.5-5 g / 10 minutes' is more preferably 2.0-8 g / 10 minutes. When this resin combination is noted, item ·

Order

13 ‘紙張尺度適用中國國家標準(CNS ) A4規格(21〇χ297公釐) 五、發明説明() 物的逾、度處於上述範圍㈣,能製得具有優異剛性 的滾塑製品七此勸旨組合物的炫體流動速率處於上^強度 時,此樹脂組合物顯示優異的可滾塑性 =圍内 觀的聚乙嬌滾朔制2。 此衣何'具有良好外 希樹脂組合妨7 66,俾 如上所述,根據本發明的用於滚塑的聚 含乙稀1-驗絲物⑴與乙_雜或乙稀。= 共聚物(Β)。 α 往此聚乙稀樹脂組合物中,可以加人添加劑,如有 機填料,抗氧化劑’熱穩定劑,紫外光吸收劑,阻燃劑, 甩劑’潤滑劑’發泡劑,著色劑,脫模劑及氣候穩定劑,所永 的量應不影響本發明的目的。 經濟部智慧財產局員工消費合作社印製 根據本發明的用於滾塑的聚乙烯樹脂組合物可以是粉末 狀或顆粒狀,而當要進行滾塑時,則此組合物只要求粉末狀。 士當根據本發明的用於滾塑的聚乙烯樹脂組合物爲顆粒狀 時,在進行滾塑之前將顆粒粉碎成爲粉末。 希望根據本發明的用於滚塑的聚乙烯樹脂組合物粉末的 粒杈不大於30目,優選爲40-1〇〇目。當使用的粉末的粒徑爲13 'The paper size applies the Chinese National Standard (CNS) A4 specification (21 × 297 mm) 5. Description of the invention () The excess and degree of the material are in the above range, and a rotomolded product with excellent rigidity can be produced. When the dazzling body flow rate of the composition is at the upper strength, the resin composition exhibits excellent roll plasticity = a polyethlenol roll system 2 which is seen from the outside. This garment has a good resin composition, and it may be 66, 俾 As described above, the polyethylene-containing 1-inspection material for rotomolding according to the present invention is mixed with ethylene or ethylene. = Copolymer (B). α To this polyethylene resin composition, additives such as organic fillers, antioxidants' heat stabilizers, ultraviolet light absorbers, flame retardants, throwing agents, lubricants, foaming agents, colorants, The amount of mold agent and weather stabilizer should not affect the purpose of the present invention. Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, the polyethylene resin composition for rotomolding according to the present invention may be powder or granular, and when rotomolding is to be performed, the composition only requires powder. When the polyethylene resin composition for rotomolding according to the present invention is in the form of granules, the granules are pulverized into a powder before being subjected to rotomoulding. It is desirable that the particle size of the polyethylene resin composition powder for rotomolding according to the present invention is not more than 30 mesh, and preferably 40 to 100 mesh. When the particle size of the powder used is

五、發明説明( 上述範園時,其可滾塑性 優異’可得到外觀良好的滚塑製 α 口 σ 得:將乙稀1卡煙共聚物;^布樹脂組合物可以如下製 稀烴共聚物(Β)以及上^)、乙烯均聚物或乙稀 如擠出機、班布裏混合機的添加劑,用通常的捏合裝置 ^ 機或漢歇爾混合機進行熔融捏 口,4財祕碎I錢械粉碎法將捏合物製成粉末。 連择進A 的用於滾塑的聚乙烯細旨組合物可通過 茂金翻烯烴聚合反應催化劑存在下將乙 原子的Γ烯烴進行共聚,以製備乙烯1, 二Κ 和在―茂金屬型或齊格勒型聚合反應催化劑存 2 _-步均聚或絲_n 3_2G個 的 製備乙錄紅烯1卡域 ^ 經濟部智慧財產局員工消費合作社印製 碎法錢械t碎法將製得的樹脂組合物製成粉末。在辦= 可以用彳“衣置將樹驗合物與添加舰概融捏合。 乂一田乙烯1-烯煙共聚物⑴和乙稀均聚物或乙歸— 烯:^共*物(B)均贿格勒㈣烴聚合反應催化劑製, 根據本發明的滾翻的聚乙烯樹脂組合物可通過連 個共聚步驟和-個触或絲步驟,織進行粉碎而製丁妓 聚是在齊格勒型烯烴聚合反應催化齡在下將乙雜個 A7 B7 五、發明説57 聚或此Ϊ t 订共聚製造乙稀―α—烯烴共聚物(A),均 聚制在狀勒輯烴聚合反應催化劑存在下將乙_ 共勿(β)或將乙烯與3,個碳原子的烴 (Β); 捏合脂組合物製成粉末。在粉碎之前可㈣ 置將树知組合物與添加劑進行熔融捏合。 行滾塑用的聚乙稀樹脂組合物可通過連續進 得:共個均聚或共聚步驟,_進行粉碎而製 3-20個物聚合反雜化齡在下將乙稀與 μ 子的進行找,以製備乙烯1-辦妓 ^ 均聚或共聚是在二茂金屬型晞烴聚合反應催化劑存 原早I歸均聚以製備乙烯均聚物⑻或將乙烯與3-20個碳 用、人、查:、物共聚’以製備乙烯—α_烯烴共聚物⑻;Ρ遺後 二^碎法或機械粉碎法將所得的樹驗合物製成粉末。在 人。㈤可㈣捏合裝置將樹脂組合物與添加劑進行溶融捏 滾塑製品 ^據本發明的滾塑製品通過將上述用於滾塑的聚乙稀樹 曰、,且&amp;物進行滾塑而製得。被進行滾塑的聚乙烯樹脂组入物, 如上所述爲粉末狀。 &quot; 16 210X297公釐) 經濟部智慧財產局員工消費合作社印製 L、發明説明( 本發明的滾塑萝〇 i田、A人、 個作搖滾運動的模罝中 +又轴方疋轉的拉具中,或放入一 内表面並溶融。然、後將,讎分佈在模具的 e槿朔制。兩山 夺柄/、々部,亚將在模具内表面形成的 柄』衣口口取出。這樣就得到了本發明的滾塑製品。 模具的内表面可以有浮雕圖案,也可以不必有。 康本,一月的滾塑用聚乙烯樹脂組合物含有兩種特別的 私―共聚物,或含有一種特別的乙烯-α-烯烴共聚 一種5烯均聚物’由這兩種(共)聚合物組成的摻混物具 ^寺疋的密度及特定的炫财動速率。因此,此聚乙稀樹脂組 5物具有優異的可滾塑性並能製出在耐衝擊性及_境應力 開衣丨生(ESOR)方面優於通常的聚乙烯模塑製品的滚塑製品。 ^根據本I明的滾塑製品由本發明的聚乙烯樹脂組合物製 付’因此本發明的滾塑製品在耐衝擊性及《環境應力開裂性 (ESCR)方面優於通常的聚乙職塑品。 因此,根據本發明的用於滾塑的聚乙稀樹脂組合物適用於 製造中空製品及形狀複雜的製品。更明確地說,本發明的聚乙V. Description of the invention (in the above-mentioned Fanyuan, it has excellent rotational plasticity, and can obtain a rotomolded α mouth σ with a good appearance. Obtained: the ethylene 1 card tobacco copolymer; ^ cloth resin composition can be prepared as follows: a dilute hydrocarbon copolymer (B) and the above additives, ethylene homopolymers, or additives such as extruders and Banbury mixers, are melt-kneaded with a common kneading device ^ or a Hanschel mixer, and 4 secrets are crushed. I The money pulverization method made the kneaded powder into powder. The polyethylene composition for rotomolding continuously selected into A can be copolymerized with ethylene atom Γ olefin in the presence of a goldlocene olefin polymerization catalyst to prepare ethylene 1, 2K, and Preparation of Ziegler-type polymerization catalysts 2 _-step homopolymerization or silk _n 3_2G preparations Ethyl redene 1 card domain Resin composition is made into powder. In operation = You can use 彳 "clothes to mix the tree test compound with the added ship. 乂 Yita ethylene 1-ene smoke copolymer ⑴ and ethylene homopolymer or ethyl return-ene: ^ co * * (B ) It is made of catalyst for homopolymerization of hydrocarbons from grelerene. The tumbling polyethylene resin composition according to the present invention can be pulverized through continuous copolymerization steps and a touch or silk step. Type olefin polymerization reaction catalyst age will be a heteroatom A7 B7 V. Inventor 57 polymerization or this order t copolymerization to produce ethylene-α-olefin copolymer (A), homopolymerization catalyst exists Next, kappa (β) or ethylene and a hydrocarbon of 3 carbon atoms (B); knead the fat composition to make a powder. Before pulverization, it can be set to melt-knead the Shuzhi composition and additives. OK The polyethylene resin composition for rotomolding can be obtained by continuous advancement: a total of homopolymerization or copolymerization steps, _ pulverization to make 3-20 objects, polymerization, dehybridization age, and then the ethylene and muons are found, To prepare ethylene 1-do prostitutes ^ Homopolymerization or copolymerization is based on the existence of a catalyst for the polymerization of dimetallocene-type hydrocarbons. Homopolymerization to prepare ethylene homopolymers or copolymerization of ethylene with 3-20 carbons to prepare ethylene-α-olefin copolymers; post-crushing or mechanical crushing The obtained dendritic compound is made into powder. In humans, the kneading device can melt the resin composition and additives to knead the rotomolded product. ^ According to the rotomolded product of the present invention, the above-mentioned polyethylene for rotomolding is prepared by The tree is said to be made by rotomolding. The rotomolded polyethylene resin composition is powder as described above. &Quot; 16 210X297 mm) Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs Making L, description of the invention (Rotomolding Roots of the present invention, A man, a rocking mold + a rotary tool, or an inner surface and melting. Then, later The cymbals are distributed in the mold of the hibiscus. The two handles and the crotch, and the handles formed on the inner surface of the mold are taken out. In this way, the rotomolded product of the present invention is obtained. The surface may be embossed or unnecessary. The ene resin composition contains two special private-copolymers, or a special ethylene-α-olefin copolymer, and a 5-ene homopolymer. A blend of these two (co) polymers is provided. Density and specific rate of wealth. Therefore, this polyethylene resin group 5 has excellent roll plasticity and can produce better impact resistance and environmental stress opening clothing (ESOR) than ordinary Rotomolded articles of polyethylene molded products. ^ The rotomolded articles according to the present invention are made of the polyethylene resin composition of the present invention. Therefore, the rotomolded articles of the present invention have impact resistance and "environmental stress cracking resistance (ESCR)". In terms of advantages, it is superior to the usual polyethylene products. Therefore, the polyethylene resin composition for rotomolding according to the present invention is suitable for manufacturing hollow products and products with complicated shapes. More specifically, the polyethylene of the present invention

請 閱 讀 注' 意 事 項Please read 'Notes'

頁 訂 線 五、 發明説明( ,樹脂組合物_於製A號的或小號 球體,園藝用品,櫥具,機械零件,且谷盗, 品,_品,料。 ”有㈣部位的中空模塑 ^考下列實施㈣本發明作進—步描述,但應該認識 到,本鲞明決不受限於這些實施例。 用於實施例及比較實施例中的乙烯—α _稀煙共聚物及乙 烯均聚物,製備如下。 α-烯烴共聚物 里二及乙烯—“ η (1) 乙烯-1-己烯共聚物(M-PE (1)) 催化劑:含錯的二茂金屬型烯烴聚合反應催化劑 密度(ASTM D1505): 0.905g/cm3 經濟部智慧財產局員工消費合作社印製 MFR (ASTM D1238,190°C,負載:2· 16Kg) : 1 克 /10分鐘 (2) 乙烯-1-己烯共聚物(Μ-PE (2)) 催化劑:含鍅的二茂金屬型烯烴聚合反應催化劑 欲度(ASTM D1505) ·· 0· 905g/cm3 MFR (ASTM D1238,19(TC,負載:2· 16Kg) : 4 克 18 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇χ297公董) 0( 5 3 9 5 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明説明() /10分鐘 (3) 乙烯-1-丁烯共聚物(Z-PE (1)) 催化劑:齊格勒型烯烴聚合反應催化劑 密度(ASTM D1505) : 0.957g/cm3 MFR (ASTM D1238,190°C,負載:2.16Kg) : 8· 3 克/10分鐘 (4) 乙烯-丙烯共聚物(Z-PE (2)) 催化劑:齊格勒型烯烴聚合反應催化劑 密度(ASTM D1505) : 0.966g/cm3 MFR (ASTMD1238,190°C,負載:2· 16Kg) : 12·5 克/10分鐘 (5) 乙烯-丙烯共聚物(Ζ-ΡΕ (3)) 催化劑:齊格勒型烯烴聚合反應催化劑 密度(ASTM D1505) : 0.970g/cm3 MFR (ASTM D1238,190°C,負載:2· 16Kg) : 16 克/10分鐘 (6) 乙烯-丙婦共聚物(Z-PE (4)) 催化劑:齊格勒型烯烴聚合反應催化劑 密度(ASTM D1505) : 0.965g/cm3 MFR (ASTM D1238,190°C,負載·· 2· 16Kg) ·· 11 克/10分鐘 (7) 乙烯均聚物(Z-PE (5)) 催化劑:齊格勒型烯烴聚合反應催化劑 本紙張尺度適用中國國家標準(CNS ) A4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁)Page Binding V. Description of the invention (, resin composition _ Yu size A or small spheres, gardening supplies, cabinets, mechanical parts, and pirates, products, products, materials. "Hollow mold with hollow parts Considering the following implementations, the present invention is further described, but it should be recognized that the present invention is by no means limited to these examples. The ethylene-α-thin smoke copolymers used in the Examples and Comparative Examples and Ethylene homopolymer was prepared as follows. Di- and ethylene in α-olefin copolymers-"η (1) Ethylene-1-hexene copolymer (M-PE (1)) Catalyst: Polymerization of di-metallocene-type olefins containing errors Reaction catalyst density (ASTM D1505): 0.905g / cm3 MFR (ASTM D1238, 190 ° C, load: 2.16Kg) printed by the Consumer Cooperatives of Intellectual Property Bureau of the Ministry of Economic Affairs: 1 g / 10 minutes (2) Ethylene-1- Hexene copolymer (M-PE (2)) catalyst: thorium-containing metallocene catalyst for olefin polymerization (ASTM D1505) ···· 905g / cm3 MFR (ASTM D1238, 19 (TC, load: 2) · 16Kg): 4 grams 18 This paper size applies to Chinese National Standard (CNS) A4 (21〇297297) 0 (5 3 9 5 Printed by A7 B7 of the Consumer Cooperatives of the Ministry of Intellectual Property Bureau of the People's Republic of China 5. Description of the invention () / 10 minutes (3) Ethylene-1-butene copolymer (Z-PE (1)) Catalyst: Ziegler-type olefin polymerization catalyst Density (ASTM D1505): 0.957g / cm3 MFR (ASTM D1238, 190 ° C, load: 2.16Kg): 8.3g / 10min (4) Ethylene-propylene copolymer (Z-PE (2)) Catalyst: Ziegler-type olefin polymerization catalyst density (ASTM D1505): 0.966g / cm3 MFR (ASTMD1238, 190 ° C, load: 2.16Kg): 12 · 5 g / 10 minutes (5) ethylene-propylene copolymer (Z -PE (3)) Catalyst: Ziegler-type olefin polymerization catalyst Density (ASTM D1505): 0.970g / cm3 MFR (ASTM D1238, 190 ° C, load: 2.16Kg): 16 g / 10 minutes (6) Ethylene-propylene copolymer (Z-PE (4)) catalyst: Ziegler-type olefin polymerization catalyst density (ASTM D1505): 0.965g / cm3 MFR (ASTM D1238, 190 ° C, load ·· 2 · 16Kg) ·· 11 g / 10 min (7) Ethylene homopolymer (Z-PE (5)) Catalyst: Ziegler-type olefin polymerization catalyst This paper is applicable to Chinese National Standard (CNS) A4 210 X 297 mm) (Please read the back of the precautions to fill out this page)

593500 A7 __ B7 五、發明説明() 密度(ASTM D1505): 0.968g/cm3 MFR (ASTM D1238,190°C,負載:2.16Kg) : 5. 2 克/10分鐘 (8) 乙烯-4-曱基-1-戊烯共聚物(z-PE (6)) 催化劑:齊格勒型烯烴聚合反應催化劑 密度(ASTM D1505) : 0· 944g/cm3 MFR (ASTM D1238,190°C,負載·· 2.16Kg) ·· 7. 1 克/10分鐘 實施例1 用直徑爲40mra的單螺杆擠出機在2〇(rc下把3〇重量份乙 烯-1-己烯共聚物(Μ-PE⑴)及7〇重量份乙稀+丁烯共聚 物(Z-PE⑴)進行熔融捏合,以製備聚乙烯樹脂組合物。 然後,將胁合物進行冷絲碎讀備_不大於目 的极人,筒狀容器中,並在模溫2 订滾塑時間條件爲:加熱時間: 分鐘’及冷卻時間:5分鐘 土情間.2 筒狀容器)。 度A 3mm的模塑品(圓 從模塑産品中取出樣品,根據下述方法 爾遜剛性試驗,懸臂帛1 丁拉伸试驗,奥 木式鱗辦’及耐環境應力開裂性試593500 A7 __ B7 V. Description of the invention () Density (ASTM D1505): 0.968g / cm3 MFR (ASTM D1238, 190 ° C, load: 2.16Kg): 5. 2 g / 10 minutes (8) Ethylene-4- 曱1-pentene copolymer (z-PE (6)) catalyst: Ziegler-type olefin polymerization catalyst density (ASTM D1505): 0 · 944g / cm3 MFR (ASTM D1238, 190 ° C, load ·· 2.16 Kg) 7.1 g / 10 minutes Example 1 A single screw extruder with a diameter of 40 mra was used at 20 (rc) to 30 parts by weight of ethylene-1-hexene copolymer (M-PE) and 7 〇Parts by weight of ethylene + butene copolymer (Z-PE⑴) are melt-kneaded to prepare a polyethylene resin composition. Then, the fibrous compound is subjected to cold-wire crushing and preparation _ not larger than the purpose, in a cylindrical container And set the rotational molding time conditions at the mold temperature 2 as follows: heating time: minutes' and cooling time: 5 minutes. (2 cylindrical containers). A 3 mm molded product (round). Samples were taken from the molded product and tested in accordance with the following methods: the Nelson's rigidity test, the cantilever cylindrical tensile test, the Austrian scale tester, and the environmental stress crack resistance test.

I 意I mean

頁 濟 部 智 慧 財 產 局 消 ♦ 合 社 印 製Page of Ministry of Economic Affairs and Intellectual Property Bureau of China

W5〇〇 驗 濟 部 智 慧 財 產 局 消 費 合 作 社 印 製 L、發明説明( 驗。所得結果列於表1。 式驗方法 (1) 拉伸試驗 根據ASTM D-638在拉伸速度5〇毫求/分鐘 m蚊產生時的應力,斷裂拉伸強度及斷裂伸長打似 (2) 奥爾遜剛性試驗 根據ASTM D-747進行奥爾遜剛性試驗。 (3)懸臂梁式衝擊試驗 根據JIS K-7110在-20°C在切口條件進行懸臂梁式衝擊試 (4)環境應力開裂試驗 根據ASTM D-1698在5(TC用權安塔羅克斯(Antarox) (CO-630)溶液進行環境應力開裂試驗。使用厚度爲gmm的樣 品。表1中的值表示的是50%斷裂時間(小時)。 實施例2 用與實施例1相同的方法製造聚乙烯樹脂組合物,不同的 是,乙烯-1-·己烯共聚物(Μ-PE (1))的用量爲40重量份,並 用60重量份乙烯—丙烯共聚物(Z-PE (2))代替70重量份乙 烯一 1—丁烯共聚物(Z-PE (1))。 21 本紙張尺度適财額家標準(CNS ) M規格(21()&gt;&lt;297公褒) C7W500 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs of the People's Republic of China, the invention description is printed. The results are shown in Table 1. Formula test method (1) Tensile test according to ASTM D-638 at a tensile speed of 50 millimeters / The stress, tensile strength at break, and elongation at break when mosquitoes are generated in minutes (2) Olson stiffness test The Olson stiffness test is performed according to ASTM D-747. (3) Izod impact test according to JIS K-7110 Izod impact test at notch condition at -20 ° C (4) Environmental stress cracking test Environmental stress cracking according to ASTM D-1698 at 5 (TC using Antarox (CO-630) solution Test. A sample with a thickness of gmm was used. The values in Table 1 indicate 50% break time (hours). Example 2 A polyethylene resin composition was produced in the same manner as in Example 1, except that ethylene-1 -The amount of hexene copolymer (M-PE (1)) is 40 parts by weight, and 60 parts by weight of ethylene-propylene copolymer (Z-PE (2)) is used instead of 70 parts by weight of ethylene-1-butene copolymer (Z-PE (1)). 21 This paper is suitable for financial standards (CNS) M specifications (21 () &gt; &lt; 297) ) C7

))

五、創作説明( θ用與貫施例1相同的方法製造聚乙烯樹脂組合物,不同的 疋’乙烯:卜己埽共聚物(Μ-PE (2))的用量爲30重量份,並 用7〇重量份乙烯烯絲物(Ζ-ΡΕ⑷)代替7(]重量份乙 烯一1-丁烯共聚物(Z-PE (1))。 請 先 閱 讀 背 然後’用與實_丨相_方式,用此聚乙烯樹脂組合物 粒禮不大於3G目的粉末’並將此粉末進行滾塑以獲得模 塑製品。 、 製 注 意 再 頁 …從模塑製品中取出樣品,以上述方法進行拉伸試驗,奥爾 遜剛性試驗,懸臂梁式衝擊試驗和環境應力開裂試驗。結果列 於表1中。 實施例5 θ用與實施例1相同的方法製造聚乙烯樹脂組合物,不同的 是’乙稀旦卜己埽共聚物(Μ—ΡΕ⑴)的用量爲25重量份,並 用75重量份乙烯均共聚物(ζ_ρΕ⑸)代替7〇重量份 丁烯共聚物(Ζ-ρε (1))。 ,然後,用與實施例1相同的方式,用此聚乙稀樹脂組合物 製備粒徑;f大於3〇目的粉末’並減縣餘_ 塑製品。 俣 23 本紙張尺度適用中關★榡率(CNS) (2獻297公董) 訂 線 經濟部智慧財產局員工消費合作社印製 —— ^93500 、發明説明( k柄塑製品中取出樣品,以上 ==驗,㈣科衝觀驗和魏應力 ίΜΜΙ 在—個聚合反應器中,在含錯二 化劑存在下,將乙烯與卜己稀進行反應催 _5)爲請4祕曝STM_ 負、^ =顶 爲1克/1G分鐘的乙稀+己稀共聚物(㈣(^)载.2馬) (M-PE (3)) 反應為串%的另-聚合反應器中,在該反應器中,在含二 茂金屬型烯烴聚合反應催化劑存在下,將乙_丨—己触^ 共聚’以製備密度(ASTM D1505)爲 〇. 957g/cm3,_ (A^ D1238 ’ 190°C,負載:2.16Kg)爲8.8克/1〇分鐘的乙稀—卜 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 己烯共聚物(Μ-PE⑷)’由它製得密度(ASTM D15〇5)爲 0. 940g/cm3,MFR (ASTMD1238,19(TC,負載:2.16Kg)爲 &amp; 9 克/10分鐘的聚乙烯樹脂組合物。在此樹脂組合物中,乙烯一卜 己烯共聚物(Μ-PE (3))與乙烯-1—己烯共聚物(M_pE (4)) 的重量比爲30/70。 然後’用與實施例1相同的方式,用此聚乙烯樹脂組合物 _____24 &quot;^紙張尺度適用中國國家標隼(CMS ) Α4規格(210Χ297公缝)— 593500 C7V. Creation instructions (θ The polyethylene resin composition was manufactured by the same method as in Example 1. The amount of the different ethylene: buhexylene copolymer (M-PE (2)) was 30 parts by weight, and 7 was used. 〇Parts by weight of vinylene filaments (Z-PEE) instead of 7 (] parts by weight of ethylene-1-butene copolymer (Z-PE (1)). Please read the back first and then the “Use and Reality_Phase_” method, Use this polyethylene resin composition to granulate powder that is not larger than 3G mesh ', and perform rotomolding on this powder to obtain a molded product.. Note the next page ... Take the sample from the molded product and perform the tensile test in the above method. Olson rigidity test, cantilever impact test, and environmental stress cracking test. The results are shown in Table 1. Example 5 θ A polyethylene resin composition was manufactured in the same manner as in Example 1, except that 'ethene The amount of the dioxin copolymer (M-PEE) was 25 parts by weight, and 75 parts by weight of the ethylene homopolymer (ζ_ρΕ⑸) was used instead of 70 parts by weight of the butene copolymer (Z-ρε (1)). In the same manner as in Example 1, using this polyethylene resin composition Prepared particle size; f greater than 30 mesh powder 'and minus county surplus _ plastic products. 俣 23 This paper size is applicable to Zhongguan ★ 榡 rate (CNS) (2 offer 297 directors). Printed-^ 93500, description of the invention (samples are taken from plastic products with k handle, the above == inspection, Peng Kehong inspection and Wei stress ΜΜΙ In a polymerization reactor, in the presence of the wrong dichemical agent, the Ethylene reacts with dihexyl _5) is a 4th exposure STM_ negative, ^ = top 1 g / 1G min ethylene + hexahexylene copolymer (㈣ (^) load. 2 Ma) (M-PE (3) In another polymerization reactor having a reaction of string%, in this reactor, in the presence of a metallocene-containing olefin polymerization catalyst, ethylene is copolymerized to prepare a density (ASTM D1505) is 0.957 g / cm3, _ (A ^ D1238 '190 ° C, load: 2.16Kg) is 8.8 g / 10 minutes, and the ethylene-copolymer printed by the consumer property cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs prints a hexene copolymer. (M-PE⑷) 'from which the density (ASTM D1505) was 0.940 g / cm3, and the MFR (ASTMD 1238, 19 (TC, load: 2.16 Kg)) was &amp; 9 g / 10 min polyethylene resin composition. In this resin composition, an ethylene-hexene copolymer (M-PE (3)) and an ethylene-1-hexene copolymer (M_pE (4)) The weight ratio is 30/70. Then 'in the same manner as in Example 1, use this polyethylene resin composition _____24 &quot; ^ Paper size is applicable to China National Standard (CMS) A4 specification (210 × 297 cm) — 593500 C7

五、創作説明( 製備粒控不大於3〇目的4八士 、, 獲得模 塑製品。 的叔末,亚將此粉末進行滾塑以 從模塑製品中取屮祥口 、、、 遜剛性試驗,懸臂梁式衝二:上$方法進订拉伸試驗,奥爾 於表丨中。 和環境應力開裂試驗。結果列 比較實施例1 用1貫施例1_的方式製備粒徑不大 不同的是用乙料甲基+戊稀共聚 例1中的聚乙烯樹脂%人胳。脸士 ☆ 八代曰貝轭 、、口物將此粉末進行滾塑以獲得模塑製 品0 、、 從模塑製品中取出樣品,以上述方法進行拉伸試驗,奥爾 遜剛性試驗,料__試驗和魏應力縣試驗。結果列 於表1中。 經濟部智慧財產局員工消費合作社印製V. Creation instructions (preparation of granules with a particle size of not more than 30 meshes and 48 mils, to obtain molded products. Uncle, Ya, this powder was subjected to rotomolding to obtain the rigidity test from the molded products. , Cantilever beam punching II: The tensile test is ordered in the above method, and is shown in Table 丨 and the environmental stress cracking test. The results are listed in Comparative Example 1. The particle size is not significantly different from the method used in Example 1_. Ethylene methyl + pentylene copolymerization was used in the polyethylene resin% 1. Face ☆ Yatsushiro yoke, this product was rotomolded to obtain a molded product 0, from the molded product Take out the sample and perform the tensile test, Olson rigid test, material test and Wei stress county test in the above method. The results are shown in Table 1. Printed by the Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs

本紙張尺度適用中國國家棣準(CNS ) A4規格(210X297公釐〉 593500 A7This paper size applies to China National Standard (CNS) A4 (210X297mm) 593500 A7

7 B 經濟部智慧財產局員工消費合作社印製 五、發明説明() 比較實施1 I 1 I 1 1 0.944 r—Η 卜· oo 實施例6 .0.904 Γ ' &lt; 0.957 〇〇 〇6 30/70 0. 940 CO 卜 i實施例5 1 0.905 τ—Η 1 i j 0.968 CNI LO 25/75 0. 951 寸 CO οα CXI 實施例4 0.950 寸 0.965 τ—Η 30/70 0.945 oo 卜· CD 實施例3 0.905 1 Ή 1 1 0.970 CO 45/55 0.940 οα CO CD 1實施例2 〇 〇\ 〇 τ—-Η 0.966 12.5 40/60 0.940 οα CO CJD 1實施例1 1 0.905 τ—Η 0. 957 CO 〇6 30/70 0.940 CO CO 卜 1· i 乙烯一 α-烯烴共聚物(A) 密度 (g/cm3) MFR (g/10 min) 乙稀均聚物或乙烯/α -烯烴 共聚物(Β) 密度 (g/cm3) MFR (g/10 min) 樹酯組分(A)與(B)的重量比 樹酯組分或樹酯性質 密度 (g/cm3) MFR (g/10 min) 滾塑製品性質 拉伸性質 破壞應力 (MPa) # (請先閱讀背面之注意事項再填寫本頁) 26 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 訂 593500 A7 B7 五、發明説明() 92 09卜7 B Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. Description of the invention () Comparative implementation 1 I 1 I 1 1 0.944 r—Η · Example oo 6.0.904 Γ '&lt; 0.957 〇〇〇6 30/70 0. 940 CO Example 5 1 0.905 τ—Η 1 ij 0.968 CNI LO 25/75 0. 951 inch CO οα CXI Example 4 0.950 inch 0.965 τ—Η 30/70 0.945 oo CD Example 3 0.905 1 Ή 1 1 0.970 CO 45/55 0.940 οα CO CD 1 Example 2 〇〇 \ 〇τ—-Η 0.966 12.5 40/60 0.940 ο α CO CJD 1 Example 1 1 0.905 τ—Η 0.957 CO 〇6 30 / 70 0.940 CO CO BU1 · i Ethylene-α-olefin copolymer (A) Density (g / cm3) MFR (g / 10 min) Ethylene homopolymer or ethylene / α-olefin copolymer (B) Density ( g / cm3) MFR (g / 10 min) Weight ratio of resin components (A) to (B) Resin component or resin property density (g / cm3) MFR (g / 10 min) Rotomolded product properties Tensile failure stress (MPa) # (Please read the precautions on the back before filling in this page) 26 This paper size applies Chinese National Standard (CNS) A4 specification (210X297 mm) Order 593500 A7 B7 V. Invention () 9209 BU

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I 009&lt; 經濟部智慧財產局員工消費合作社印製 (%)I 009 &lt; Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs (%)

SM (s) (m/f) (Jq) SS3 。雜镩K-l«s^^^^d,p,l&lt;co 。荽命黑鸽奪客鬲 。荽娱餘邋竣客£)令崩^(5令戚^^學#荽^奧鹊|#銮9-1:#嫁駟.1 (赞雄) (請先閲讀背面之注意事項再填寫本頁)SM (s) (m / f) (Jq) SS3. Miscellaneous K-l «s ^^^^ d, p, l &lt; co. Kill the black dove to win customers.荽 Entertainment is completed 邋) Ling Bang ^ (5 令 戚 ^^ 学 # 荽 ^ 奥 鹊 | # 銮 9-1: # 婚 驷 .1 (Zanxiong) (Please read the notes on the back before filling out this page)

、1T 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐)、 1T This paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm)

Claims (1)

593500 鉍 · C8 ---— _ D8 六、申請專利範圍 1 種滾塑用的聚乙細樹脂組合物,其特徵是它包含: (A) 含有乙烯及帶3-20個碳原子的α —烯烴的乙烯—j一 稀烴共聚物,其密度(ASTM D15〇5)爲〇. 88〇_〇. 93〇g/cm3,熔 體流動速率(MFR) (ASTM D1238,19(TC,負載:2. 16Kg)爲 0.01-5克/10分鐘,及 (B) 含有乙烯的乙烯均聚物或含有乙烯及帶3_2〇個碳原 子的α-烯烴的乙烯一α-烯烴共聚物,其密度(ASTM D1505) 爲 〇· 931-0· 974g/cm3,熔體流動速率(MFR) (ASTMD1238,190 C,負載:2· 16Kg)爲 0· 5-20 克/10 分鐘, 其中, 乙烯一 α-烯烴共聚物(A)與乙烯均聚物或乙烯一 α一烯 烴共聚物(Β)的重量比〔(A) / (Β)〕爲10/90-50/50,及 由乙稀一 α-婦烴共聚物(Α)與乙稀均聚物或乙烯一 α-烯烴 共聚物(Β)組成的摻混物的密度(ASTM D1505 )爲 〇· 920-0· 960g/cm3,熔體流動速率(MFR) (ASTM D1238,190 °C,負載:2· 16Kg)爲 1-10 克/10 分鐘。 2·如申請專利範圍第1項所述的滾塑用的聚乙烯樹脂組合 物’其中乙稀一α-烯烴共聚物(A)、乙稀均聚物(B)及乙稀 —α-烯烴共聚物(β)均是用二茂金屬型烯烴聚合反應催化劑 製備的。 . 3·如申請專利範圍第1項所述的滾塑用的聚乙烯樹脂組合 ___ —_28 _____ _ 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁) 訂- 經濟部智慧財產局員工消費合作社印製 六、申請專利範圍 =應:1::烯煙共聚物⑴是用二茂金屬型稀烴聚合 丑H、聚物’而乙稀均聚物⑻及乙燦1 -稀煙 、來(B)是用齊格勒型驗聚合反應催化難備的。 ^•如申請專利範圍第1項所述的滾翻的聚乙稀樹脂組合 物’ *t乙烯~α-稀烴共聚物⑷、乙稀均聚物⑻及乙稀 α〜烯共雜⑻是用齊格勒㈣烴聚合反應催化劑製備 的。 5·如申請專利範圍第1項所述的滚塑用的聚乙烯樹脂組合 物’其中乙烯一 α-烯烴共聚物(A)是用齊格勒型烯烴聚合反 應催化劑製備的,而乙烯均聚物(B)及乙烯一 烯烴共聚物 (Β)是用二茂金屬型烯烴聚合反應催化劑製備的。 6 ·如申請專利範圍第1-5項中的任一項所述的聚乙烯樹脂組 合物,其中該聚乙烯樹脂組合物的粉末粒徑不大於30目。 7 · —種滾塑製品,包含申請專利範圍第1_5項中任一項所述 的滾塑用的聚乙稀樹脂組合物。 8· —種滾塑製品,包含申請專利範圍第6項所述的滾塑用的 聚乙烯樹脂組合物。 29 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) &gt;1 - I ! 1 —· (請先閲讀背面之注意事項再填寫本頁) 訂 經濟部智慧財產局員工消費合作社印製593500 Bismuth · C8 --- _ D8 VI. Application for Patent A type of polyethylene resin composition for rotomolding, which is characterized in that it contains: (A) α-containing ethylene and 3-20 carbon atoms — Ethylene-j-dilute hydrocarbon copolymer of olefins, its density (ASTM D1505) is 0.888-0.993 g / cm3, melt flow rate (MFR) (ASTM D1238, 19 (TC, load: 2. 16Kg) is 0.01-5 g / 10 minutes, and (B) an ethylene homopolymer containing ethylene or an ethylene-α-olefin copolymer containing ethylene and an α-olefin with 3_2 carbon atoms, and its density ( (ASTM D1505) is 0.931-0.974g / cm3, and the melt flow rate (MFR) (ASTMD1238, 190 C, load: 2.16Kg) is 0.5-20 g / 10 minutes, in which ethylene-α- The weight ratio [(A) / (B)] of the olefin copolymer (A) to the ethylene homopolymer or the ethylene-α-olefin copolymer (B) is 10 / 90-50 / 50, and the ethylene-α- The density (ASTM D1505) of the blend consisting of the olefin copolymer (A) and ethylene homopolymer or ethylene-α-olefin copolymer (B) is 920 · 920-0 · 960g / cm3, and the melt flow rate (MFR) (ASTM D1238, 1 90 ° C, load: 2.16Kg) is 1-10 g / 10 minutes. 2. The polyethylene resin composition for rotomoulding according to item 1 of the patent application scope, wherein the ethylene-α-olefin copolymer (A), ethylene homopolymer (B) and ethylene-α-olefin copolymer (β) are all prepared by using a metallocene-type olefin polymerization catalyst. 3. As described in item 1 of the scope of patent application Polyethylene resin combination for rotomolding ___ —_28 _____ _ This paper size applies to China National Standard (CNS) A4 specification (210X297 mm) (Please read the precautions on the back before filling this page) Order-Ministry of Economic Affairs Printed by the Consumer Cooperative of the Property Bureau. 6. Scope of patent application = should be 1: 1 :: ene smoke copolymer ⑴ is a diene metallocene-type dilute hydrocarbon polymerized ugly H, polymer ', and ethylene homopolymer ⑻ and Echan 1- Dilute smoke and carbon (B) are difficult to prepare with Ziegler-type polymerization polymerization. ^ • Rolled polyethylene resin composition as described in item 1 of the scope of patent application * * ethylene ~ α-dilute hydrocarbon Copolymers ⑷, ethylene homopolymers ⑻, and ethylene α ~ ene co-heterocycles are prepared using Ziegler ㈣ hydrocarbon polymerization catalysts 5. The polyethylene resin composition for rotomoulding according to item 1 of the scope of the patent application, wherein the ethylene-α-olefin copolymer (A) is prepared using a Ziegler-type olefin polymerization catalyst, and ethylene The homopolymer (B) and the ethylene-olefin copolymer (B) are prepared using a metallocene-type olefin polymerization catalyst. 6. The polyethylene resin composition according to any one of claims 1 to 5, wherein the powder particle diameter of the polyethylene resin composition is not greater than 30 mesh. 7 · A rotomolded product comprising the polyethylene resin composition for rotomolding according to any one of claims 1 to 5 of the scope of patent application. 8 · — A rotomolded product comprising the polyethylene resin composition for rotomolding according to item 6 of the scope of patent application. 29 This paper size applies the Chinese National Standard (CNS) A4 specification (210 × 297 mm) &gt; 1-I! 1 — · (Please read the precautions on the back before filling this page) Printed by the Intellectual Property Bureau Employee Consumer Cooperatives system
TW89113425A 1999-07-16 2000-07-06 Polyethylene resin composition for rotational molding and rotational molded product using the composition TW593500B (en)

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