TW387919B - Propylene-ethylene copolymer, preparation thereof and molding thereof - Google Patents

Propylene-ethylene copolymer, preparation thereof and molding thereof Download PDF

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Publication number
TW387919B
TW387919B TW86100102A TW86100102A TW387919B TW 387919 B TW387919 B TW 387919B TW 86100102 A TW86100102 A TW 86100102A TW 86100102 A TW86100102 A TW 86100102A TW 387919 B TW387919 B TW 387919B
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Taiwan
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propylene
ethylene
unit
copolymer
molecular weight
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TW86100102A
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Chinese (zh)
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Jun Saito
Hisafumi Kawamoto
Akiko Kageyama
Koichi Hatada
Yoshiyuki Oki
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Chisso Corp
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Abstract

This invention provides propylene-ethylene copolymer which gives a molding having an excellent heat resistance and film having both heat sealing in low temperature and rigidity, preparation thereof and molding. A propylene-ethylene copolymer comprising 0.01-15 mol% of ethylene unit, characterized in that in a chain structure in accordance with nuclear magnetic resonance spectrum, triad fraction (PEP), triad fraction (EEE) and <alpha>, <beta>-methylene carbon number fraction (N<alpha><beta>) are in a specific scope; the weight average molecular weight is 50000-1500000, and the distribution of molecular weight is 1.2-3.8. Said copolymer can be prepared by copolymerizing ethylene with propylene in the presence of a catyst comprising a combination of a specific chiral transition metal compound (metallocene) and aluminoxane.

Description

經濟部中央揉率局貝工消费合作杜印裂 A7 B7五、發明説明(1 ) 發明所11枋谢節疃 本發明係鼷於丙烯-乙烯共聚物,尤指具有特戡之乙 烯單元鏈,丙烯單元的異種鍵最搔少,且分子1分佈狹 小的丙烯-乙烯共聚物,及其製法。 另關於此丙烯-乙烯共聚物成型所得成型品。 習佑知抟街 晋知丙烯-乙烯共聚物具有結晶性較直鐽結晶性聚丙 烯均聚物為低,且玻璃化溫度亦低之特激,廣用於薄膜 等範«,惟在其他應用範糖受到限制,為在此等範_應 用,亟需提高各種特性。 例如,連最廣用的薄膜範疇中,基於節省能源的觀點 ,要求低溫熟封性,習用上是採取降低共聚物融點.的方 法,而犧牲薄膜的晒性•故亟需能兼顧相抵觸的明性和 低溫熱封性。 此等習知丙烯-乙烯共聚物,通常是採用钛觸媒,將 乙烯和丙烯共聚合製成,惟此共聚合方法所得丙烯-乙 烯共聚物諸特性的改菩有限•近年來就採用觴媒糸不同 的二络金屬和鋁氧烷姐合醣媒,將烯烴(共)聚合的烯烴 (共)聚合物製法,進行各種研究。 例如採用具有特定構造的矽交脚型二铬金靥和鋁氧烷 構成的觸媒,將丙烯聚合而得高度立體規則性聚丙烯, 分子量分佈狭,融點高,且刚性高,已如特開平3-12406 和 3-1 2407號,及 &lt;〈化學通信 &gt;&gt;(pp.1853-1856,1989) 所載,惟未具髖揭示丙烯—乙烯共聚物之技術。 一 3 - (請先閲讀背面之注意事項再填寫本頁) 裝· -訂 r 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) A7 B7 鋰濟部中央搮準局貝工消费合作社印製 五、發明説明(2 ) 另外,筒井等人觀察到使用乙烯雙(1-茚基)二氯化皓 和甲基鋁氧烷組成的觸媒糸,將丙烯和乙烯共聚合所得 丙烯-乙烯共聚物,κ二個丙烯單元的內消旋鍵單元 (BB;二價基)所規定的立體規則性,即使與習知鈦糸觸 媒成份所得共聚物相同,惟此二络金麗-鋁氧烷系觸媒 所得丙烯-乙烯共聚物融點,仍較钛系觸媒成份所得共 聚物為低,原因是二絡金羼-鋁氧烷系觸媒所得丙烯-乙 烯共聚物中,有許多丙烯簞元的異種鐽之故(筒井等人 ’&lt;&lt;聚合物&gt;&gt;,30, 1 350 (1 989))。此丙烯單元的異種 鍵多,使用钛系觭媒的丙烯聚合,幾乎是藉1,2插入反 應而進行聚合,相對地,使用此等公知二络金鼷觭媒進 行丙烯聚合反應,成為Μ —定比率進行2,1插入反懕和 1,3插入反應。 發明所箱麻決的謙雜 按照習知技術,丙烯-乙烯共聚物,用於例如薄_等 成型材料時,很難兼顔良好削性和低溫熱封性。 本發明之目的,在於提·供兼顧良好蜊性和低溫热封性 的丙烯-乙烯共聚物,及其製法,Μ及此共聚物之成型 品。 本發明人等為達成上述目的潛心研究结果,成功製造 具有乙烯單元特戡性鐽,極少丙烯單元異種鍵量,且分 子1分佈狭的丙烯-乙烯共聚物,並發現具有由此製法 所得特定構造的丙烯-乙烯共聚物,不但可製成兼具良 好剛性和低溫熱封性的薄膜,或射熱性更優的射出成翠 -4- 本柝依尺度適用中國圃家揉準(CNS &gt; Μ規格(2丨0X297公釐) s'. (請先閲讀背面之注意事項再填寫本頁) 、tx. 經濟部中央標準局貝工消費合作社印製 A7 B7 五、發明説明(5 ) 品,且成型性亦佳,而完成本發明。 阚决課顗的丰段 本發明第一要旨是提供一種丙烯-乙烯共聚物,包括 乙烯單元0 . 0 1〜1 5莫耳;K和丙烯單元99 . 9 9〜8 5莫耳!ϋ ,其特擞為; (a) 由核磁共振譜的鐽構造為: (a-Ι)在共聚物主鐽的三個單體鍵單元(三價基)中, 丙烯單元-乙烯單元-丙烯單元相連的分率(PEP)與全乙 烯單元含量(C2)之間,圼下式(I)關係: 0.0070X C2-0. 0020S PEP^ 0.0070X C2 + 0.0130(1 ) 和(a-2)在共聚物主鏈的三個單體鐽單元(三價基)中, 乙烯單元三連的分率(EEE)與全乙烯單元含量(C2)之間 ,圼下式(I )關係: EEE^ 0.00033X C2 + 0.0010 ( I ) 且,U-3)相對於全丙烯單元,全α, /9-亞甲碳數比率 (Ηα召)在0〜1.2莫耳《範圍, (b) 重量平均分子量(Mw)為5 0,000〜1,500,000, Κ 及 U)重量平均分子量(Mw)與數平均分子量(Μη)之比 (Μ&quot;Μη )為 1 . 2〜3 . 8。 本發明第二要旨為上述第一要旨丙烯-乙烯共聚物之 製法,其特徵為,在通式(1)所示旋光性過渡金羼化合物 和鋁氧烷組成的觸媒存在下,將乙烯和丙烯共聚合: -5- 本紙張尺度適用中國國家搮準(CNS ) Α4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁)The Central Government Bureau of the Ministry of Economic Affairs, Shellfish Consumption Cooperation, Du Yinhe A7 B7 V. Description of the Invention (1) Inventory 11 (Xie Jie) The invention is based on propylene-ethylene copolymers, especially ethylene unit chains with special characteristics. A propylene-ethylene copolymer having the fewest heterogeneous bonds of a propylene unit and a narrow distribution of molecule 1 and a method for producing the same. The molded article obtained by molding this propylene-ethylene copolymer is also mentioned. Xiyou Zhijie Street knows that propylene-ethylene copolymers have lower crystallinity than straight crystalline polypropylene homopolymers, and have extremely low glass transition temperatures. They are widely used in films and other applications, but in other applications Due to limitations, in order to be used in such applications, various characteristics need to be improved. For example, in the category of the most widely used films, from the viewpoint of energy conservation, low-temperature curing properties are required. Conventionally, a method of reducing the melting point of the copolymer is adopted, and the sacrifice of the films is sacrificed. Therefore, it is necessary to take into account the conflict Brightness and low temperature heat sealability. These conventional propylene-ethylene copolymers are usually made by copolymerizing ethylene and propylene using a titanium catalyst. However, the properties of the propylene-ethylene copolymers obtained by this copolymerization method have been limited. • In recent years, rhenium media have been used.研究 Various methods for preparing olefin (co) polymers by olefin (co) polymerization with different dicomplex metals and aluminoxane glycosides. For example, using a catalyst consisting of a silicon cross leg type dichromium arsine and alumoxane with a specific structure, propylene is polymerized to obtain highly stereoregular polypropylene, with a narrow molecular weight distribution, high melting point, and high rigidity. Kaiping Nos. 3-12406 and 3-1 2407 and &lt; &lt; Chemical Communications &gt; &gt; (pp. 1853-1856, 1989), but there is no technology for revealing propylene-ethylene copolymers. 1 3-(Please read the notes on the back before filling in this page) Binding ·-Ordering This paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm) A7 B7 Printed by the cooperative V. Description of the invention (2) In addition, Tsutsui et al. Observed the use of a catalyst consisting of ethylene bis (1-indenyl) dichloride and methylalumoxane to copolymerize propylene and ethylene. -Ethylene copolymer, the stereoregularity specified by the meso bond unit (BB; divalent radical) of two propylene units of κ, even though it is the same as the copolymer obtained from the conventional titanium-rhenium catalyst component, -The melting point of the propylene-ethylene copolymer obtained from the alumoxane-based catalyst is still lower than that of the copolymer obtained from the titanium-based catalyst component. There are many heterogeneous species of propylene units (Ttsui et al. '&Lt; Polymers &gt;, 30, 1 350 (1 989)). There are many heterogeneous bonds in this propylene unit. The polymerization of propylene using titanium-based rhenium is almost polymerized by 1, 2 insertion reaction. In contrast, the propylene polymerization reaction using these well-known diluent gold sulfonates becomes M — A fixed ratio of 2,1 insertion reaction and 1,3 insertion reaction. Modestness of the box hemp according to the invention According to the conventional technique, when a propylene-ethylene copolymer is used in a molding material such as thin, it is difficult to achieve both good cutting and low-temperature heat-sealability. The object of the present invention is to provide and provide a propylene-ethylene copolymer having good clam properties and low-temperature heat-sealability, a method for producing the same, and a molded product of the copolymer. In order to achieve the above-mentioned objective, the inventors made intensive research results, successfully produced a propylene-ethylene copolymer having ethylene unit specific properties, very few heterogeneous bond amounts of propylene units, and a narrow distribution of molecule 1, and found that it has a specific structure obtained by the production method. Propylene-ethylene copolymer, not only can be made into a film with both good rigidity and low-temperature heat-sealability, or injection with better heat radiation performance. This standard is suitable for Chinese gardeners (CNS &gt; Μ specifications (2 丨 0X297mm) s'. (Please read the precautions on the back before filling this page), tx. Printed by A7 B7, Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (5) And the moldability is also good, and the present invention has been completed. The first gist of the present invention is to provide a propylene-ethylene copolymer including ethylene units of 0.01 to 1.5 moles; K and propylene units of 99 9 9 ~ 8 5 Mol! Ϋ, its special 擞 is: (a) The 鐽 structure of the nuclear magnetic resonance spectrum is: (a-1) three monomer bond units (trivalent radicals) in the main 鐽 of the copolymer In the propylene unit-ethylene unit-propylene unit connection (PEP), The relationship between the olefin unit content (C2) and the following formula (I): 0.0070X C2-0. 0020S PEP ^ 0.0070X C2 + 0.0130 (1) and (a-2) three monomers in the main chain of the copolymer In the unit 价 (trivalent base), the ratio of the triplet (EEE) of the ethylene unit and the total ethylene unit content (C2) has the following formula (I): EEE ^ 0.00033X C2 + 0.0010 (I) and, U-3) The ratio of the total α, / 9-methylene carbon number (Ηαcall) to the range of 0 to 1.2 mol with respect to the all propylene unit, (b) the weight average molecular weight (Mw) is 5 0,000 to 1,500,000, Κ And U) The ratio (M &quot; Mη) of the weight average molecular weight (Mw) to the number average molecular weight (Μη) is 1.2 to 3.8. The second gist of the present invention is the method for producing a propylene-ethylene copolymer according to the first gist, which is characterized in that, in the presence of a catalyst composed of an optically active transition metal compound represented by the general formula (1) and an alumoxane, ethylene and Copolymerization of propylene: -5- This paper size applies to China National Standard (CNS) Α4 size (210X297 mm) (Please read the precautions on the back before filling this page)

經濟部中央標準局負工消费合作社印装 A7 _ B7 五、發明説明(4 ) /(孓ιΗ卜鼸只*·)\ /X Q Μ (1)Printed by the Central Standards Bureau of the Ministry of Economic Affairs and Consumer Cooperatives A7 _ B7 V. Description of Invention (4) / (孓 ιΗ 卜 鼸 只 * ·) \ / X Q Μ (1)

\ ( C * Η 4-n R \ Y\ (C * Η 4-n R \ Y

I 式中,M為選自鈦、皓和給的過渡金鼷原子,X和Y相 同或不同,為氫原子、鹵素原子或烴基, (H 4-m R^m ) 和(C5H“n R2n )為被取代環戊二烯基,其中R 1和R 2相 同或不同,為Ci _ 2〇烴基,可與環戊二烯的環上二個 碳原子结合形成一K上的烴環,亦可K烴基取代,或為 含矽烴基,π和n為1〜3整數,Q為選自烴基、未被取 代甲矽烷叉基和烴取代甲矽烷叉基,可將((^Ν-ιπΙ^ιη ) 和(C5H“nR2n &gt;交聯之二價基。 另外,本發明第三要旨之特徵為,Μ上述第一要旨的 丙烯-乙烯共聚物為成型材料,加Κ成型之成型品。 链明》當施形雔 本發明第一要_的丙烯-乙烯共聚物中,共聚物的鐽 構造,即全乙烯單元含量(C2),單體的鐽單元分率(PEP) 和(EEE) , K及全α,/?-亞甲碳數,是採用聚合物澹度 20重悬ίί的鄹二氣苯/多溴化苯二=18/2軎量比的混合 溶液,利用核磁共振在67.20MHz, 130t:測得结果所 計算值。测定裝置可例如使用Jeol-GX270 NMR测定裝置 (曰本電子公司製品)。 本發明第一要旨的丙烯-乙烯共聚物,含乙烯單元〇.〇1 至15萁耳5K , K0.05至12莫耳3!為佳,而Μ 〇.〇5至10莫 耳χ尤佳。全乙烯簞元含量在〇.〇1莫耳》κ下時•共聚 一 6 - 本产張Α度適用中國國家標準(CNS ) ( 210Χ297公釐) C ·^ In- tm ϋ^ι HI -»1 ^^^1 1¾ In (請先閲讀背面之注意事項再填寫本頁) 訂 經濟部中央標準局貝工消費合作社印裝 A7 B7 五、發明説明(5 ) 物會失去本特性,而超出15莫耳Si時,共聚物的结晶性 會降低,Μ致耐熱性下降。 在本說明中所用,於丙烯-乙烯共聚物主鐽中的三個 單體鐽單元(三價基)中,「丙烯單元4乙烯單元—丙烯 單元相連的分率(PEP)」和「乙烯單元三連的分率(EEE)j 用語,指角五等所提議(&lt;&lt; 巨分子&gt;&gt;,1 5, 1 1 50 (1 982 )) 利用UC核磁共振譜所測得丙烯-乙烯共聚物主鍵中三價 基單元中丙烯和乙烯鏈分別為:「丙烯單元々乙烯單元 ~&gt;丙烯單元相連時的分率(PEP)」,和「乙烯單元—乙 烯單元4乙烯單元,三個乙烯單元相連時的分率(EEE)」 ,在本發明第一要旨中,就13 C核磁共振譜的高峰歸靨, 也是根據角五等的上述提議決定。 « 本發明第一要旨的丙烯-乙烯共聚物中,丙烯單元4 乙烯單元4丙烯單元相連之分率(PEP),在共聚物主鏈 中全丙烯-乙烯單元中,顧及三連的單體鍵單元(三價基) 時,為丙烯單元4乙烯單元4丙烯單元相鐽的鼸單充對 全三價基鐽單元之存在比率,三價基分率(PEP)愈高, 夾在丙烯單元間的孤立乙烯單元比率,即無規性愈高。 本發明第一要旨的丙烯-乙烯共聚物中,丙烯單元— 乙烯單元—丙烯單元相鏈的分率(PEP),與共聚物中全 乙烯單元含量(C2,單元是萁耳S:)之間,呈式(I)之關 係: 0.0070X C2-0.0020S PEPS 0.0070X C2 +0.0130(1 ) 以式(I’)之瞄係為佳: -7- 本纸張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) * . Jrt m· ml m ml ΙΜΊ· ^^^^1 ·ϋν&gt; Lv/ i^i^— (請先閱讀背面之注意事項再填寫本頁)In the formula, M is a transition gold atom selected from titanium, Hao, and X, X and Y are the same or different, and are a hydrogen atom, a halogen atom, or a hydrocarbon group, (H 4-m R ^ m) and (C5H "n R2n ) Is a substituted cyclopentadienyl group, wherein R 1 and R 2 are the same or different and are Ci — 20 hydrocarbon groups, which can be combined with two carbon atoms on the ring of cyclopentadiene to form a hydrocarbon ring on K, and It may be substituted by K hydrocarbon group, or a silicon-containing hydrocarbon group, π and n are integers of 1 to 3, Q is selected from hydrocarbon group, unsubstituted silylidene group and hydrocarbon substituted silylidene group, and ((^ N-ιπΙ ^ ιη) and (C5H "nR2n &gt; crosslinked divalent group. In addition, the third aspect of the present invention is characterized in that the propylene-ethylene copolymer of the first aspect is a molding material, and a molded product formed by adding K. Chain "Ming" when the shape of the propylene-ethylene copolymer of the first aspect of the present invention, the copolymer structure, namely the total ethylene unit content (C2), the monomer unit ratio (PEP) and (EEE), K and the total α, /?-Methylene carbon number are a mixed solution of trifluorene / polybrominated benzene = 18/2 at a polymer ratio of 20 and resuspended, using nuclear magnetic resonance at 67.20 MHz, 1 30t: Calculated value of the measurement result. The measurement device may be, for example, a Jeol-GX270 NMR measurement device (manufactured by Bento Electronics Co., Ltd.). The propylene-ethylene copolymer of the first aspect of the present invention contains ethylene units of 0.01 to 15%. Ears 5K, K0.05 to 12 Moore 3! Is preferred, and M 0.05 to 10 Moore χ is particularly preferred. When the content of all ethylene fluorene is below 0.01 Moore κ, a copolymerization of 6- Zhang A degree of this product applies Chinese National Standard (CNS) (210 × 297 mm) C · ^ In- tm ϋ ^ ι HI-»1 ^^^ 1 1¾ In (Please read the precautions on the back before filling this page) Order Printed by the Central Standards Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperatives, printed A7 B7 V. Description of the invention (5) When the material exceeds 15 mol Si, the crystallinity of the copolymer will decrease, and the heat resistance will decrease. As used in the description, among the three monomer units (trivalent radicals) in the main unit of the propylene-ethylene copolymer, "propylene unit 4 ethylene unit-propylene unit connection fraction (PEP)" and "ethylene unit triple connection (EEE) j term, which refers to the angle five proposals (&lt; &lt; Giant molecule &gt; &gt;, 1, 5, 1 1 50 (1 982)) using the UC core The propylene and ethylene chains in the trivalent unit of the main bond of the propylene-ethylene copolymer measured by the resonance spectrum are: "propylene unit 々 ethylene unit ~ &gt; fraction when the propylene unit is connected (PEP)", and "ethylene unit- In the first gist of the present invention, the peak of the 13 C nuclear magnetic resonance spectrum is summarized according to the above-mentioned proposal of Cang Wu and so on. «In the propylene-ethylene copolymer of the first aspect of the present invention, the propylene unit 4 ethylene unit 4 propylene unit connected fraction (PEP), the full propylene-ethylene unit in the copolymer main chain, taking into account the triple bond When the unit (trivalent base) is the ratio of the existence of 鼸 single charge to the full trivalent base 鐽 unit in the propylene unit 4 ethylene unit 4 propylene unit, the higher the trivalent base fraction (PEP), the more it is sandwiched between propylene units. The higher the ratio of isolated ethylene units, the higher the randomness. In the propylene-ethylene copolymer of the first aspect of the present invention, the fraction of the propylene unit-ethylene unit-propylene unit phase chain (PEP) and the total ethylene unit content in the copolymer (C2, the unit is SS :) The relationship of the formula (I): 0.0070X C2-0.0020S PEPS 0.0070X C2 +0.0130 (1) It is better to use the aiming system of formula (I '): -7- This paper standard applies to the Chinese National Standard (CNS) A4 size (210X297mm) *. Jrt m · ml m ml ΙΜΊ · ^^^^ 1 · ϋν &gt; Lv / i ^ i ^ — (Please read the precautions on the back before filling this page)

、^T 經濟部中央樣準局貝工消費合作社印製 A7 B7五、發明説明(6 ) · 0.0070X C2$ PEPS 0.0070X C2 + 0.0130(1 ') 而Μ式(I ”)之關係最好 0.0070X C2S PEPS 0.0070X C2 + 0.0090(1 &quot;) 丙烯單元—乙烯單元4丙烯單元相連的分率(PEP)超 出上式(I)的丙烯-乙烯共聚物,在本發明技術範圍内 尚未發規。另方面,(PEP)分率過小時,由共聚物所得 薄膜之低溫熱封性惡化。 另方面,乙烯單元三鰱的分率(EEE)在共聚物主鍵中 的全丙烯和乙烯單元當中,顧及三連單體的鐽單元(三 價基)時,乙烯單元乙烯單元乙烯單元的乙烯單元 三連之鏈單元,相對於全三價基鐽單元的存在比率是, 三價基分率(EEE)愈高,乙烯單元在共聚物中嵌段的存 在比率愈高。 本發明第一要旨的丙烯-乙烯共聚物中,乙烯單元— 乙烯單元4乙烯單元相連分率(EEE),與共聚物中全乙 烯單元含量((C2),單元為萁耳《 )之間,圼式(I)闞 係: ΕΕΕ^ 0.00033Χ C2 + 0.0010 ( Π ) Μ式(《 *)關係為佳: 0.00033Χ C2-0.0028S EEES 0.00033Χ C2 + 0.0005(H ’) 而K式U”)翡係尤佳: 0.00033X 02-0.00022^ ΕΕΕ^ 0.00033Χ C2 ( I &quot;) 乙烯單元4乙烯單元乙烯單元相連的分率(EEE), 較上式(I)範圍為大時,由共聚物所得薄膜的低溫热封 -8- (請先閲讀背面之注意事項再填寫本頁) •-α·, ^ T Printed by A7 B7, Shellfish Consumer Cooperative of the Central Sample Bureau of the Ministry of Economic Affairs 5. Description of the invention (6) · 0.0070X C2 $ PEPS 0.0070X C2 + 0.0130 (1 '), and the relationship of M formula (I) is the best 0.0070X C2S PEPS 0.0070X C2 + 0.0090 (1 &quot;) Propylene unit-ethylene unit 4 The propylene unit connected fraction (PEP) exceeds the propylene-ethylene copolymer of the formula (I) above, which has not yet been issued within the technical scope of the present invention. On the other hand, when the (PEP) fraction is too small, the low-temperature heat-sealability of the film obtained from the copolymer is deteriorated. On the other hand, the fraction of the ethylene unit triplet (EEE) is all propylene and ethylene units in the main bond of the copolymer. Among them, when taking into account the tritium unit (trivalent radical) of the trivalent monomer, the existence ratio of the trivalent chain unit of the ethylene unit ethylene unit ethylene unit relative to the full trivalent radical unit is the trivalent radical fraction. The higher the (EEE), the higher the block existence ratio of the ethylene unit in the copolymer. In the propylene-ethylene copolymer of the first aspect of the present invention, the ethylene unit-ethylene unit 4 ethylene unit connection fraction (EEE) is copolymerized with Content of all ethylene units ((C2), unit is 萁Between "), the formula (I) is: ΕΕΕ ^ 0.00033 × C2 + 0.0010 (Π) The formula (" *) has a better relationship: 0.00033 × C2-0.0028S EEES 0.00033 × C2 + 0.0005 (H ') and K type U ") Fei series is particularly preferable: 0.00033X 02-0.00022 ^ ΕΕΕ ^ 0.00033 × C2 (I &quot;) Ethylene unit 4 Ethylene unit The ethylene unit is connected to the ethylene unit (EEE), which is larger than the range of the above formula (I) At the time, the low temperature heat sealing of the film obtained from the copolymer-8- (Please read the precautions on the back before filling this page) • -α ·

,tT • HI. (210X297公釐) 經濟部中央標準局貝工消费合作社印製 A7 B7 五、發明説明(7 ) 性會惡化。另方面,(EEE)分率過小時,在本發明技術 範藺內尚未發現。 在本發明者,全ex, &gt;3-亞甲磺數對全丙烯單元含量 (C3)的比率(Να/8),根據筒井等人提案(&lt;〈聚合物〉〉 30, 1 350 ( 1989 ))之方法,為利用13 C核磁共振譜測得 丙烯-乙烯共聚物主鐽中,全α ,/9 -亞甲碳數對全丙烯 單元含量(C3)的存在比率(Hct/3,單位為萁耳J!), 為同一文獻中定義的數值之100倍。此值反映出 ,持續丙烯的2,卜插入反應,並非基於肇因於丙烯的1, 2-插入反應和乙烯的插入反應之α,/?-亞甲碳譜.而是 肇因於共聚物中丙烯的2,1-插入反應之異種鍵量。 本發明第一要旨的丙烯-乙烯共聚物在六鐽中,相對 於全丙烯單元含量(C3,單位為莫耳)的α,/3-亞甲碳 數(單位為其耳)之比率Ua/3),在〇〜1.2莫耳5;範 圍,M0〜0.5莫耳5;為佳,而K0〜0.2萁耳X尤佳。共 聚物主鐽中相對於全丙烯單元含量(C3,單位為萁耳) 的亞甲碳數(單位為莫耳)之比率(Ηαθ)過大 時,共聚物成型體的剛性和低溫熱封性會降低。 » 本發明第一要旨的丙烯-乙烯共聚物,幾乎丙烯的異 種鍵存在,而具有由於乙烯單元無規结合於共聚物中的 共聚物主鐽之鍵構造存在。 本發明第一要旨的丙烯-乙烯共聚物的重最平均分子 量(MW)和數平均分子量(Μη),是Μ聚合物澹度0.05重量 X的鄰二氛苯溶液,藉凝膠透過性曆析法(G PC),使再 -9- 本纸張尺度通用中國國家標準(CNS ) A4说格(210X297公釐) - &quot;Λ 1. — - H - - - - _ K_ n (請先聞讀背面之注意事項再填寫本頁), tT • HI. (210X297mm) Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (7) The sex will deteriorate. On the other hand, the (EEE) fraction is too small and has not been found in the technical scope of the present invention. In the present inventors, the ratio of total ex, &gt; 3-methylenesulfonate number to total propylene unit content (C3) (Nα / 8), according to Tsutsui et al. (&Lt; <Polymer >> 30, 1 350 ( 1989)) method, using 13 C nuclear magnetic resonance spectroscopy to measure the ratio of the total α, / 9 -methylene carbon number to the total propylene unit content (C3) in the main propylene-ethylene copolymer (Hct / 3, The unit is 萁 耳 J!), Which is 100 times the value defined in the same reference. This value reflects that the continuous 2,2 insertion reaction of propylene is not based on the α, /?-Methylene carbon spectrum due to the 1, 2- insertion reaction of propylene and the insertion reaction of ethylene. It is due to the copolymer The amount of heterogeneous bonds in the 2,1-insertion reaction of propylene. The ratio of the propylene-ethylene copolymer of the first gist of the present invention to the α, / 3-methylene carbon number (in ears) of the total propylene unit content (C3 in mols) Ua / 3), in the range of 0 to 1.2 Mor 5; M0 to 0.5 Mor 5; preferably, K0 to 0.2 Mor X. When the ratio (Ηαθ) of the methylene carbon number (in moles) to the total propylene unit content (C3 in moles) in the main copolymer of the copolymer is too large, the rigidity and low-temperature heat-sealability of the copolymer molded body Will decrease. »The propylene-ethylene copolymer according to the first aspect of the present invention has a heterocyclic bond of propylene, and has a main structure of a copolymer in which ethylene units are randomly incorporated in the copolymer. The weight-average molecular weight (MW) and number-average molecular weight (Mη) of the propylene-ethylene copolymer of the first gist of the present invention are ortho-dibenzobenzene solutions with an M polymer degree of 0.05 weight X, and are analyzed by gel permeability. (G PC), make the standard of this paper -9- Common Chinese National Standard (CNS) A4 grid (210X297 mm)-&quot; Λ 1. —-H----_ K_ n (Please first listen (Read the notes on the back and fill out this page)

、1T B7_ 五、發明説明(β ) 混合聚苯乙烯凝暖管柱(例如東麗公司製PSKgel 6MB 6-HT)在135Oi«定結果》測定裝置可用例如GPC-150C (俄塔斯公苛製品)* 本發明第1要旨的丙烯-乙烯共聚物,重量平均分子 -量(M W ) 5 0,0 〇|G ~ 1,5 0 0,0 0 0,以 1 0 0,0 0 0 〜1 , 0 0 0,0 0 0 範 困為佳。 重置平均分子量(Mw)遇大時,因共聚物的熔髏流動性 降低,成型性下降,過小時,成型物的強度會降低。 本發明第一要旨的丙烯-乙烯共聚物,重量平均分子 量(Mw)對數平均分子量(Μη)之比(Mw/Mn)為1.2〜3.8, 以1 . 5〜3 . 5為佳β 此重量平均分子暈對數平均分子量(Μη)之比(Η w/ Μη),為分子量分佈的尺度,此比(Hw/Mn)太大時,分子 量分佈會太寬,則共聚物成型所得薄膜的低溫熱封性會 惡化。另方面,(Mw/MnUb在1.2以下的丙烯-乙烯共聚 物,在本發明技術範函内尚未發庚》 經濟部中央揉準局負工消费合作社印製 (請先Μ讀背面之注意事項再填寫本頁) —..... -— * — i 本發明第一要旨的丙烯-乙嫌共聚物,肇因於具有其 構迆上的特激,丙烯-乙烯共聚物的熔點(Τι)與共聚物 中全乙烯單元含量(C2,單位為莫耳X )間,呈式(瓜、 所示關僳: -8.IX C2 + 156.0-&gt;Tb-+-4.4X C2+160.0 (ffi ) 按照構造條件,具有式(m Μ所示颶像: -7 . 2 X C2 + 1 56 . 0-» Tin-» -4 . 9 X C2 + 165.0 ( m ') 尤其是式(mi所示鼷傜·· -10- · 本於張尺度適用中國國家揉準(CNS ) A4規格(210X297公釐) Μ濟部中央揉準局員工消费合作社印家 A7 B7 五、發明説明(9 ) -6 . 3 X C2 +1 56 . 0彳 Tm·^ -5.4 X C2 + 165.0 (丨&quot;) 此融點係使用DSC7型示差掃描熱量分析計(帕金美瑪 公司製品),將丙烯-乙烯共聚物從室溫,在30t: /分 鐘的升溫條件下·升溫到230 t:,在此保持10分鐘後, K-20t:/分鐘降溫到-20C,於此保持10分鐘後,在20 C/分鐘升溫條件下,顯示融解時最大吸热量的高峰溫 度之值。 本發明第一要旨的丙烯-乙烯共聚物製法,只要所得 丙烯-乙烯共聚物可符合前述各要件,並無特別限制, 惟K本發明第二要旨的使用特定二络金厲觸媒為宜。 在本發明第二要旨中,使用旋光性进渡金羼化合物和 鋁氧烷組合的觸媒,做為特定二络金靥。 可做為二絡金鼷者,有通式0)所示旋光性過渡金麗化 合物: /CsH “爾 Q Μ (1)、 1T B7_ V. Description of the invention (β) Mixed polystyrene condensing heating pipe column (for example, PSKgel 6MB 6-HT manufactured by Toray) at 135Oi «Fixed result» The measuring device can be used, for example, GPC-150C ) * The propylene-ethylene copolymer of the first gist of the present invention has a weight average molecular-weight (MW) 5 0,0 〇 | G ~ 1,5 0 0,0 0 0, and 1 0 0,0 0 0 to 1 , 0 0 0, 0 0 0 Fan is better. When the reset average molecular weight (Mw) is large, the melt flowability of the copolymer is reduced, and the moldability is reduced. If it is too small, the strength of the molded product is reduced. The propylene-ethylene copolymer of the first gist of the present invention has a weight average molecular weight (Mw) log average molecular weight (Mη) ratio (Mw / Mn) of 1.2 to 3.8, preferably 1.5 to 3.5. Β This weight average The molecular halo log average molecular weight (Μη) ratio (Η w / Μη) is a measure of the molecular weight distribution. When this ratio (Hw / Mn) is too large, the molecular weight distribution will be too wide. Sealing will deteriorate. On the other hand, (propylene-ethylene copolymers with Mw / MnUb below 1.2 have not yet been published in the technical model letter of the present invention. "Printed by the Central Consumer Bureau of the Ministry of Economic Affairs, the Consumer Cooperatives (Please read the precautions on the back before (Fill in this page) — — .. — — * — i The propylene-ethylene copolymer of the first gist of the present invention is due to its special structure, the melting point of the propylene-ethylene copolymer (Ti) And the total ethylene unit content in the copolymer (C2, the unit is Moore X), the formula (melon, shown as follows: -8.IX C2 + 156.0- &gt; Tb-+-4.4X C2 + 160.0 (ffi ) According to the structural conditions, it has a hurricane of the formula (m Μ: -7. 2 X C2 + 1 56. 0- »Tin-» -4. 9 X C2 + 165.0 (m)鼷 傜 ·· -10- · This book is applicable to the Chinese National Standards (CNS) A4 specifications (210X297 mm) on the Zhang scale. Μ The Central Consumer Standards Bureau of the Ministry of Economic Affairs of the People's Republic of China Consumer Cooperatives A7 B7 5. Invention Description (9) -6 3 X C2 +1 56. 0 彳 Tm · ^ -5.4 X C2 + 165.0 (丨 &quot;) This melting point is a DSC7 differential scanning calorimeter (product of Parkin Mima Co.), which copolymerizes propylene and ethylene. From room temperature Under the temperature rising condition of 30t: / min, and the temperature rising to 230t :, after holding for 10 minutes, the temperature of K-20t: / minute is reduced to -20C, and after holding for 10 minutes, under the temperature rising condition of 20C / minute It shows the value of the peak temperature of the maximum heat absorption during melting. The method for producing a propylene-ethylene copolymer according to the first gist of the present invention is not particularly limited as long as the obtained propylene-ethylene copolymer can meet the foregoing requirements. In the second gist, it is appropriate to use a specific diluoxin catalyst. In the second gist of the present invention, a catalyst combining a combination of optically active gold tincture compound and alumoxane is used as the specific dioxin tincture. It can be used as For the two complexes, there is an optically active transition gold compound represented by the general formula 0): / CsH "Er Q Μ (1)

^(C.H^nRV^^Y 式中Μ為選自钛、结和給之過渡金屬原子,χ和γ相同 或不同,為氬原子、齒素原子或烴基α5Η4-πιΐΛη )和 (C5H4-n θη)表示被取代環戊二烯基,其中R1和Ρ相 同或不同,為Cl - 2〇烴基,可與環戊二烯環上二個碳 原子结合形成1K上的烴環,堪可Μ煙取代,或含矽烴 基,m和η為1至3整數,Q為選自烴基,非取代甲矽 烷叉基或烴取代甲矽烷基,可與(C5H4-m )和 • -11- 本紙張尺度適用中國國家標準(CNS ) Λ4規格(21 〇Χ297公釐) h ^ « ^^^^1 Β4·-— ϋ eMmmlt a^la— (請先閲讀背面之注意事項再填寫本頁) -'β.^ (CH ^ nRV ^^ Y where M is selected from the group consisting of titanium, junction, and given transition metal atoms, χ and γ are the same or different, and are argon, halogen, or hydrocarbyl α5Η4-πιΐΛη) and (C5H4-n θη ) Represents a substituted cyclopentadienyl group, in which R1 and P are the same or different and are Cl-20 hydrocarbon groups, which can be combined with two carbon atoms on the cyclopentadiene ring to form a hydrocarbon ring on 1K. Or silicon-containing hydrocarbon group, m and η are integers of 1 to 3, Q is selected from hydrocarbon group, unsubstituted silylidene group or hydrocarbon-substituted silyl group, and can be used with (C5H4-m) and • -11- This paper size applies Chinese National Standard (CNS) Λ4 specification (21 〇 × 297 mm) h ^ «^^^^ 1 Β4 · -— ϋ eMmmlt a ^ la— (Please read the precautions on the back before filling out this page) -'β.

C A7 B7 五、發明説明(10 ) (C5H“nR2n),交取之二價基。 較佳過渡金鼷化合物是,在通式0〉中Μ為锆或給原子 ,R1和R2相同或不同,為“ -20烷基,Χ和Υ相同 或不同,為鹵素原子或烴基,Q為二烷基甲矽焼叉基。 通式0)所示旋光性過渡金屬化合物具體例,有消旋二 甲基甲矽烷叉雙(2-甲基-4,5,6,7-四氫茚基)二氯化結 〈消旋二甲基甲砂烷叉雙(2 -甲基-4,5,6, 7-四氫茚基) 二甲基踏、消旋亞甲雙(2-甲基-4,5 ,6,7-四氫茚基)二 氛化給、消旋二甲基甲矽烷叉雙(2-甲基-4-苯基茚基) 二氛化锆、消旋二甲基甲矽烷叉雙(2-甲基-4-苯基茚基) 二甲基鋁、消旋二甲基甲矽烷叉雙(2-甲基-4-笨基茚基) 二氯化給、消旋二甲基甲矽烷叉雙(2-甲基-4-桊基茚基) 二氯化锆、消旋二甲基甲矽烷叉雙(2-甲基-4-萘基茚基) 二甲基鋁、消旋二甲基甲矽烷叉雙(2-甲基-4-萘基茚基) 二氯化給、二甲基甲矽烷叉(2 ,4 -二甲基環戊二烯基)(3’ ,5·-二甲基環戊二稀基)二氯化鈦、二甲基甲矽垸叉(2, 4-二甲基環戊二烯基)(3·,5'-二甲基環戊二烯基)二氯 化i告、二甲基甲矽烷叉(2, 4-二甲基環戊二烯基)(3 ’,5 ’ 經濟部中央橾準局員工消費合作社印裝 (請先閲讀背面之注意事項再填寫本頁) -二甲基環戊二烯基)二甲基锆、二甲基甲矽烷叉(2,4-二甲基環戊二烯基)(3·,5’-二甲基環戊二烯基)二氯化 給、二甲基甲矽烷叉(2, 4-二甲基環戊二烯基)(3·,5'-二甲基環戊二烯基)二甲基給、二甲基甲矽烷叉(2,3,5-三甲基環戊二烯基)(2’,4’,5’-三甲基環戊二烯基二)二 氯化钛、二甲基甲矽烷叉(2,3,5-三甲基環戊二.稀基)(2· -12- 本^張尺度適用中國國家標準(CNS ) A4*y&amp;· ( 210X297公釐) 經濟部中央標準局員工消費合作社印裝 A7 B7 五、發明説明(11) ,4’,5’-三甲基環戊二烯基)二氛化锆、二甲基甲矽烷叉 (2, 3 ,5-三甲基環戊二烯基)(2’,4’,5'-三甲基環戊二烯 基)二甲基锆、二甲基甲矽烷叉(2,3,5-三甲基環戊二烯 基)(2',4’,5· -三甲基環戊二烯基)二氯化給、二甲基甲 矽烷叉(2,3,5-三甲基環戊二烯基)(2’,4’,5*-三甲基環 戊二烯基)二甲基給等。 此等過渡金臑化合物當中較佳者為: 二甲基甲矽烷叉(2,4-二甲基環戊二烯基)(3’,5'-二 甲基環戊二烯基)二氯化锆, 二甲基甲矽烷叉(2,4-二甲基環戊二烯基)(3’,5'-二 甲基環戊二烯基)二甲基锆, 二甲基甲矽烷叉(2,4-二甲基環戊二烯基)(3’,5’-二 甲基環戊二烯基)二氯化給, 二甲基甲矽烷叉(2,4-二甲基環戊二烯基&gt;(3',5'-二 甲基環戊二烯基)二甲基給, 二甲基甲矽烷叉(2,3,5 -三甲基環戊二烯基)(2',4', 5’-三甲基環戊二烯基)二氯化絡, 二甲基甲矽烷叉(2,3,5-三甲基環戊二烯基)(2',4’, 5’-三甲基環戊二烯基)二甲基皓, 二甲基甲矽烷叉(2,3,5-三甲基環戊二烯基)(2’,4’, 5’-三甲基環戊二烯基)二氯化給, 二甲基甲矽烷叉(2,3,5-三甲基環戊二烯基)(2',4', 5 ·-三甲基環戊二烯基)二甲基給, 此等旋光性二络金鼷在合成時,有副產非旋光性構造 -13- 本紙張尺度適用中國國家揉準(CNS ) Α4規格(21 ΟΧ 297公釐) , η SI- m a^i.— HY ml 1^1 (請先閱讀背面之注意事項再填寫本頁)C A7 B7 V. Description of the invention (10) (C5H "nR2n), the divalent radical to be handed over. The preferred transition metal compound is that in the general formula 0> M is zirconium or a given atom, R1 and R2 are the same or different Is a "-20 alkyl group, X and Y are the same or different, are a halogen atom or a hydrocarbon group, and Q is a dialkylsilylidene group. Specific examples of the optically active transition metal compound represented by the general formula 0) include racemic dimethylsilylidenebis (2-methyl-4,5,6,7-tetrahydroindenyl) dichloride Dimethylmethanesarane bis (2-methyl-4,5,6,7-tetrahydroindenyl) dimethyl step, racemic methylenebis (2-methyl-4,5,6,7 -Tetrahydroindenyl) di-atomization, racemic dimethylsilylidene bis (2-methyl-4-phenylindenyl) di-atomized zirconium, racemic dimethylsilylidene bis (2- Methyl-4-phenylindenyl) dimethylaluminum, racemic dimethylsilylidene bis (2-methyl-4-benzylindenyl), dichloro, mesodimethylsilylidene Bis (2-methyl-4-fluorenylindenyl) zirconium dichloride, racemic dimethylsilylidene bis (2-methyl-4-naphthylindenyl) dimethyl aluminum, racemic dimethyl Methylsilylidenebis (2-methyl-4-naphthylindenyl), dichlorosilylidene, dimethylsilylidene (2,4-dimethylcyclopentadienyl) (3 ', 5 ·- Dimethylcyclopentadienyl) titanium dichloride, dimethylsilylidene (2,4-dimethylcyclopentadienyl) (3,5'-dimethylcyclopentadienyl ) Dichloride, dimethylsilylidene (2, 4-dimethyl Cyclopentadienyl) (3 ', 5' Printed by the Consumer Cooperatives of the Central Bureau of Quasi-Economic Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling out this page)-Dimethylcyclopentadienyl) Dimethyl Zirconium, dimethylsilylidene (2,4-dimethylcyclopentadienyl) (3,5'-dimethylcyclopentadienyl) dichloride, dimethylsilylidene ( 2,4-dimethylcyclopentadienyl) (3,5'-dimethylcyclopentadienyl) dimethyl, dimethylsilylidene (2,3,5-trimethyl Cyclopentadienyl) (2 ', 4', 5'-trimethylcyclopentadienyldi) titanium dichloride, dimethylsilylidene (2,3,5-trimethylcyclopentadiene (Dilute base) (2 · -12- This standard is applicable to the Chinese National Standard (CNS) A4 * y &amp; · (210X297 mm) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs, printed A7 B7 V. Invention Description (11) , 4 ', 5'-trimethylcyclopentadienyl) di-zirconium zirconium, dimethylsilylidene (2, 3,5-trimethylcyclopentadienyl) (2', 4 ', 5'-trimethylcyclopentadienyl) dimethyl zirconium, dimethylsilylidene (2,3,5-trimethylcyclopentadienyl) (2 ', 4 ', 5 · -trimethylcyclopentadienyl) dichloride, dimethylsilylidene (2,3,5-trimethylcyclopentadienyl) (2', 4 ', 5 * -Trimethylcyclopentadienyl) dimethyl etc. Preferred among these transition gold compounds are: dimethylsilylidene (2,4-dimethylcyclopentadienyl) (3 ', 5'-dimethylcyclopentadienyl) dichloride Zirconium, dimethylsilylidene (2,4-dimethylcyclopentadienyl) (3 ', 5'-dimethylcyclopentadienyl) dimethylzirconium, dimethylsilylidene (2,4-dimethylcyclopentadienyl) (3 ', 5'-dimethylcyclopentadienyl) dichloride, dimethylsilylidene (2,4-dimethylcyclo Pentadienyl &gt; (3 ', 5'-dimethylcyclopentadienyl) dimethyl, dimethylsilylidene (2,3,5-trimethylcyclopentadienyl) ( 2 ', 4', 5'-trimethylcyclopentadienyl) dichloride, dimethylsilylidene (2,3,5-trimethylcyclopentadienyl) (2 ', 4 ', 5'-Trimethylcyclopentadienyl) dimethyl, dimethylsilylidene (2,3,5-trimethylcyclopentadienyl) (2', 4 ', 5' -Trimethylcyclopentadienyl) dichloride, dimethylsilylidene (2,3,5-trimethylcyclopentadienyl) (2 ', 4', 5 · -trimethyl Cyclopentadienyl) dimethyl During synthesis, there is a by-product non-optical structure-13- This paper size is applicable to the Chinese National Standard (CNS) Α4 size (21 〇 × 297 mm), η SI- ma ^ i.— HY ml 1 ^ 1 (please first (Read the notes on the back and fill out this page)

、1T 五、發明説明(I2 ) Α7 Β7 的内消旋體二絡金靥的情形,在實際使用上,不必要全 部為旋光性二絡金廳,即使混有内消旋體亦無礙。惟使 用與内消旋體之混合物時,雖視内消旋體的混倉量和丙 烯-乙烯共聚合活性而定,惟從內消旋體聚合的雜連聚 合物,可例如利用溶劑萃取等已知方法除去,所得丙烯 -乙烯共聚物可符合本發明第一要旨之要件。 此等旋光性二络金鼷可就此與鋁氧烷組合為觸媒,惟 亦可承載於微粒狀載體上。此等微粒狀載體為無機或有 機化合物,可用粒徑5〜300// b,最好是10〜200wm的 粒狀或球狀微粒固體。 用做載體的無機化合物有Si02 、Al2 〇3 、MgO、 Τί02 、ZnO等及其混合物或複合化合物,例如Si02-A1 2 〇 3 ' SiO 2 -HgO ' SiO 2 -TiO 2、SiO 2 -A1 2 0 a -Mg〇等。其中KSi02或AI2 〇3為主成份者較佳。 另外,用做載體的有機化合物有乙烯、丙烯、1-丁烯 、4-甲基-卜戊烯等(:2 - 12 α-烯烴聚合物或共聚物, 苯乙烯聚合物或共聚物。 本發明第二要旨的丙烯_乙烯共聚物製法中,做為觸 媒成份與旋光性過渡金鼷化合物組合之鋁氧烷,為通式 in. -- - --- n 1- IJ1 In - -· (請先閲讀背面之注意事項再填寫本頁) ,,τ 經濟部中央揉準局員工消費合作社印製1T 5. Invention description (I2) In the case of the meso-dioxin gold tincture of A7 B7, in practice, it is not necessary that all of the meso-dioxin gold hall is used, even if mixed with the meso-body. However, when using a mixture with a meso, although it depends on the amount of the meso and the propylene-ethylene copolymerization activity, the heteropolymers polymerized from the meso can be extracted by solvent, etc. Removal by known methods, the resulting propylene-ethylene copolymer can meet the requirements of the first gist of the present invention. These optically active di-complexes can be combined with alumoxane as a catalyst, but they can also be carried on a particulate carrier. These particulate carriers are inorganic or organic compounds, and granular or spherical particulate solids with a particle size of 5 to 300 // b, preferably 10 to 200 wm can be used. The inorganic compounds used as the carrier include Si02, Al2O3, MgO, Τ02, ZnO, etc., and mixtures or composite compounds thereof, such as Si02-A1 2 〇3 'SiO 2 -HgO' SiO 2 -TiO 2, SiO 2 -A1 2 0 a -Mg0 and the like. Among them, KSi02 or AI2 03 is preferred. In addition, organic compounds used as the carrier include ethylene, propylene, 1-butene, 4-methyl-pentene, and the like (: 2-12 α-olefin polymer or copolymer, styrene polymer or copolymer. In the propylene-ethylene copolymer manufacturing method of the second gist of the invention, the aluminoxane, which is a combination of a catalyst component and an optically active transition metal compound, has the general formula in.----- n 1- IJ1 In--·· (Please read the precautions on the back before filling out this page), τ Printed by the Staff Consumer Cooperative of the Central Bureau of the Ministry of Economic Affairs

I /IV 示 所 η 或I / IV shows η or

A t s R 物OA 合 一 化f, igA—Ro 機-C 有1A t s R OA combined f, igA—Ro machine-C has 1

R )ρ H A —οR) ρ H A —ο

•R -14- 本/紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) A7 B7 經濟部中央揉準局貝工消费合作社印製 五、發明説明(15 ) 式中^為^ - 6烴基,KCl - 4為佳,具體例有 甲基、乙基、丙基、丁基、異丁基、戊基、己基等烷基 ,烯丙基、2-甲基烯丙基、丙烯基、異丙烯基、2-甲基 -1-丙烯基、丁烯基等烯基,環丙基、環丁基、環戊基 、環己基等環烷基,和芳基等。其中Μ烷基為佳,各 R 3可相同或不同。 ' Ρ為4至30整數,Μ6至30為佳,而W8至30尤佳。 此等鋁氧烷不但一種,亦可二種Κ上组合使用,堪可 併用三甲基鋁、三乙基鋁、三異丙基鋁、三異丁基鋁、 二甲基氯化鋁等鋁氧鋁化合物。 鋁氧烷可在已知的各種條件下調製。具體例有Μ下方 法: (1) 令三烷基鋁,使用甲苯、乙醚等有機溶劑,與直接 水反應之方法; (2) 令三烷基鋁與具有结晶水的馥類,例如硫酸銅水合 物、硫酸鋁水合物反應之方法; @含三烷基鋁與矽凝膠等含浸的水份反應之方法; ⑷令三甲基鋁與三異丁基鋁混合,使用甲苯、乙醚等 有機溶劑,與直接水反應之方法: (5) 令三甲基鋁與三異丁基鋁混合,與具有結晶水的鹽 類,例如硫酸銅水合物、硫酸鋁水合物反應之方法; (6) 於矽凝膠等含浸水份,與三異丁基鋁反應後,再與 三甲基鋁反應之方法。 本發明第二要旨的丙烯-乙烯共聚物製法中,雖可使 -15- (請先閲讀背面之注意事項再填寫本頁)• R -14- This standard / paper size applies to Chinese National Standard (CNS) A4 specification (210X297 mm) A7 B7 Printed by the Central Government Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, V. Invention Description (15) where ^ is ^- 6 hydrocarbyl, KCl-4 is preferred. Specific examples include alkyl such as methyl, ethyl, propyl, butyl, isobutyl, pentyl, hexyl, allyl, 2-methylallyl, and propenyl. , Isopropenyl, 2-methyl-1-propenyl, butenyl and other alkenyl groups, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl and other cycloalkyl groups, and aryl groups. Among them, M alkyl group is preferable, and each R 3 may be the same or different. 'P is an integer from 4 to 30, M6 to 30 is preferred, and W8 to 30 is particularly preferred. These alumoxanes are not only one type, but also two types of alkoxides can be used in combination. It is possible to use trimethyl aluminum, triethyl aluminum, triisopropyl aluminum, triisobutyl aluminum, and dimethyl aluminum chloride together. Oxyaluminum compounds. The alumoxane can be prepared under various known conditions. Specific examples include the following methods: (1) a method in which trialkylaluminum is reacted with direct water using an organic solvent such as toluene, diethyl ether, etc .; (2) a trialkylaluminum is reacted with amidines having crystal water, such as copper sulfate Method for reaction of hydrate and aluminum sulfate hydrate; @Method for reaction of trialkylaluminum with impregnated moisture such as silica gel; ⑷Mix trimethylaluminum with triisobutylaluminum and use organic compounds such as toluene and ether Solvent and direct water reaction method: (5) Method of mixing trimethylaluminum with triisobutylaluminum and reacting with salts with crystal water, such as copper sulfate hydrate, aluminum sulfate hydrate; (6) A method in which water is impregnated with silicon gel and the like, reacts with triisobutylaluminum, and then reacts with trimethylaluminum. In the propylene-ethylene copolymer production method of the second gist of the present invention, although -15- (please read the precautions on the back before filling this page)

K 裝·K equipment

,1T 4 本紙張Α度適用中國國家標準(CNS ) Α4说格(210Χ 297公釐.) 趣濟部中央榡準局工消費合作杜印*. A7 B7 五、發明説日月(l4 ) 用前述二络金靥和鋁氧烷組合之觸媒,惟各觴媒成份的 用量是,相對於二絡金靥中過渡金羼原子1冥耳,鋁氧 烷中的鋁原子為10〜1 00,000莫耳,以50〜50, 000為佳, 而以100〜30, 000莫耳的範圔尤佳。 在本發明第二要旨中,於上述組合而得觸媒存在下, \ . 將丙烯和乙烯共聚合,即可製成本發明第一要旨之丙烯 -乙烯共聚物,惟聚合方法可用公知的丙烯(共)聚合製 程,例如在丁烷、戊烷、己烷、庚烷、辛烷等脂肪族烴 ,環戊烷、瓌己烷、甲基環己烷等脂環族烴,甲苯、二 甲苯、乙基笨等芳香族烴,堪有汽油餾份或加氡紫油箱 份等惰性溶輒中,將丙烯和乙烯聚合之漿液聚合法,以 及使用丙烯本身為溶劑,加Μ整體共聚合,而在氣相中 實施丙烯和乙烯的共聚合之氣相共聚合方法均可。 另外,共聚合可以連鑛式、分批式或f分批式各種方 式實施。 丙烯和乙烯共聚合時,上述觸媒可將二辂金鼷和绍氧 烷兩成份預筅混合於惰性溶劑中,供至共聚合反應糸, 亦可將二络金酾和鋁氧烷分別供應至共聚合反應糸。再 者,可在丙烯和乙烯共聚合之前,對二絡金藺和鋁氧燒 姐合的觸媒,Μ惰性溶劑中的少量α-烯烴,具體而言, 二铬金鵾中每一莫耳過渡金靨,令α-烯烴0,001〜1〇公 斤左右聚合反應後,將觭媒預活化後,再實施丙烯和乙 烯的共聚合,最後得丙烯-乙烯共聚物良好粒子,亦具 成效。 -16- 本¥張尺度適用中國國家揉率(CNS ) Α4規格(210X297公釐) ' ---- (請先閲讀背面之注$項再填寫本頁) £ 裝_ 訂 鍾濟,中央揉準局属工消费合作杜印製 A7 _ ._B7___ 五、發明説明(15 ) 可用於預活化的0C-烯烴,有C2 -12的Ot-烯經,具 體例有乙烯、丙烯、丁烯、戊烯、己烯、辛烯、4_甲基 -1-戊烯等,尤K乙烯、丙烯、4-甲基-1-戊烯為佳。 本發明第二要旨中,若在預活化.觸媒存在下,利用前 逑象合法進行丙烯和乙烯共聚合時,共聚合條件可採用 通常已知旋光性糸觸媒以聚合丙烯的同樣聚合條件。即 聚合湛度-50至150t:, JW-10至100P為佳,聚合壓力為 大氣壓至7MPa, K0.2至5MPa為佳,將丙烯和乙烯供應 至聚合器內,通常實施1分鐘至20小時左右的共聚合反 應。 又,聚合時和習知共聚合方法一樣,可添加缠量氫以 控制分子量。 在丙烯和乙烯共聚合結束後,可視需要經公知的觴媒 失活處理步驟、觴媒殘渣去除步驟、乾嫌步驟等後處理 步驟,製得本發明第一步软的丙烯-乙烯共聚物。 本發明第二要旨的丙烯-乙烯共聚物製法中,於前逑 二铬金屬和鋁氧烷組合的觸媒存在下,將乙烯和丙烯共 聚合,在丙烯插入反應之際,控制1,2-插入反應,幾乎 不發生異捶鐽,另方面,在乙烯插入反應時,會抑制乙 烯的連鑛性插入反應,則乙烯單元更無規地结合於共聚 物中。 結果,在本發明第二要旨的丙烯-乙烯共聚物製法宁, 可得支持乙烯單元更加無規结合的單體鐽,具有極少的 丙烯單元異種鍵量,且分子量分析狹的本發明第一要旨 -17- 本紙張Λ度適用中國國家標準(CNS )A4规格(210X297公嫠) (請先閲讀背面之注項再填寫本頁) -s^_ . 經濟部中央搮率局里消费合作社印装 A7 _ _B7___五、發明説明(16 ) 之丙烯-乙烯共聚物。 在本發明第三要旨的成型品中,僳於本發明第一要旨 的丙烯-乙烯共聚物,視需要混配抗氣化劑、紫外線吸 收劑、抗靜電剤、成核劑、潤清劑、難燃劑、防封閉剤 、着色«、無機質或有機質之充填《等各種添加播,以 及各種合成樹脂,呈粉末狀態,或使用熔混機,在190 〜35QeC溫度,加熱熔混20秒至30分鐘左右0,再切成 粒狀形成顆粒狀態,供做成型材料》 成型法可以採用各種己知聚丙烯成型法,例如射出成 型、壓出成型、發泡成型、中空成型等,由此等方法可 製得各種工業用射出成型組件,各種容器、無延伸膜、 單軸延伸膜、雙軸延伸膜、Η材、管、纖維等各種.成型 品β 音偷例 本發明可藉實施例和比較例進一步詳述β m丙樣-7,樣#琚_&gt;雜诰 奩掄拥1 設備傾斜葉片並附設撗拌器而内容稹為10 OdB3的不 銹網製聚合器,以氮氣排淨後,在聚合器内,於20eC gi 度加料正己烷50dn 3,甲基鋁氣烷的甲苯溶液(東蘇愛 科蘇公司製品,商品名MMA0,濃度2id(d·3),換算成 鋁原子為2.0·〇1,以及旋光性二甲基甲矽烷叉(2,3,5 -三甲基琛戊二烯基)(2·,4·,5'-三甲基璣戊二烯基)二 氰化姶0.09毫莫耳和内消旋體二甲基甲矽烷叉(2,3,5- -1 8 - (請先閲讀背面之注$項再壤寫本頁) Κ 裝· 钉 本产張尺度逋用中國國家標準(CNS〉Α4規格(210X297公釐〉 A7 B7 五、發明説明(17 ) 三甲基環戊二烯基)(2·,3.,5,-三甲棊環戊二稀基)二氣 化給0.01毫奠耳之混合物,做為二絡金靥,連同甲苯 0 · 5 d a 3 〇 接著,聚合器內升溫至45υ後,將丙嫌93.9莫耳χ , 乙烯6.0莫耳χ和氫o.i莫耳χ组成的混合氣體,以 8dm3 /rain供應速度,連鑛供應至聚合器內,保持聚合 器内溫度451C,將聚合器内氣相部存在的混合氣篇一部 份,從另行安裝於聚合器内氣相部的閥,連績排出聚合 器外,Μ保持壓力0.4M Pa,進行丙嫌和乙稀共聚合4小 時。 經濟部中央橾準局員工消费合作社印衷 (請先聞讀背面之注意事項再填寫本頁) 聚合反應结束後,將未反應丙烯、乙稀和氣,從聚合 器內放出,取2-丙醇3dm 3投人聚合器內,在30t:携拌 10分鐘,使觸媒失活。再添加氛化氫水溶液(濃度12ind/ dm3 &gt;0.2dm3和甲酵8dm3 ,在60¾處理30分鐘。處理 完舉後,停止攪拌,從聚合器下方除去水相部份,添加 同量的氯化氫水溶液和甲酵,重複同樣操作。其次,添 加氫氧化納水溶液(濃度5!11〇丨/€||113)0.02(1113,水2&lt;1||13 和甲醇2dm3,在30¾攪拌處理10.分鐘。處理後,停止 攪拌,從聚合器下方除去水相部份後,再加水8dm3, 在30 t:授拌處理10分鐘,除去水相部份的操作重複二次 後,從聚合器取出聚合物漿液、過漶、乾燥,得丙烯-乙烯共聚物2.4公斤,做為實施例1的評估試樣。 當啪俐2 將實施例1所用正己烷,改用甲苯50dm 3為聚合溶劑 -19- 本紙張尺度逍用中國國家揉率(CNS ) A4規格(210X297公釐) A7 B7 五、發明説明(18) ,供應聚合器的混合氣體姐成份為,丙烯90. 5莫耳》:、 乙烯9.5莫耳、氫/0 ,聚合溫度為30C,其餘按實 胞例1同樣條件,製造丙烯-乙烯共聚物,得實施例2 評估試樣。 —啻豳俐3 供至聚合器内的混合氣體組成為:丙烯96.8奠耳X 、 乙烯3.2箕耳S: 、·氫0 ,且聚合溫度50*0,餘按實施例1 同樣條件,製成丙烯-乙烯共聚物,得實施例3評估試 樣。 g敝例4 將實施例1所用正己烷,改用甲苯50dm3 ,做為聚合 溶劑,而供至聚合器內的混合氣體組成為,丙烯84.8莫 耳!《 、乙烯15.1萁耳V,和氫〇.1莫耳,餘按實施例 1同樣條件,製造丙烯-乙烯共聚物,得實豳例4評估 試樣6 經濟部中夬標準局貝工消費合作社印製 (請先聞讀背面之注意事項再填寫本頁) 使用二甲基甲矽烷叉(2,3,5-三甲基環戊二烯基)(2’, 4!,5'-三甲基環戊二烯基)二氯化鉻0.09毫莫耳和二甲 基甲矽烷叉(2,3,5-三甲基環戊二烯基)(2’,3’,5’-三甲 基環戊二烯基)二氯化結0.01毫莫耳的混合物,做為二 絡金鼷,而供至聚合器内的混合氣體姐成為,丙烯91.1 莫耳S;、乙烯8.8萁耳S;、氫0.1其耳3J ,餘按實胞例 4同樣條件,實施丙烯-乙烯共聚合和共聚物精製後, 從聚合器取出含共聚物之溶劑部份。 本产•珉尺度適用中國國家標率(CNS ) Μ規格(210X297公嫠) /.· 五、發明説明(19 A7 B7 經濟部中央揉丰局貝工消费合作杜印裝 取出的溶劑中溶有共聚物 全部,此溶液裝入溶劑滅壓 齡除裝置,於滅jg下· η;-. ' ’ ® 701:餾除95¾甲笨後,冷卻到 25¾..投人甲酵之以·3 把 ’_出共聚物,進行過漶和乾燥 ,製造丙烯-乙烯共聚物 得實胞例5評估試樣0 fch » 俐 1 將實施例1所用觴媒卜^ 媒(〜铬金属和甲基鋁氧烷),改用 氯化续承載型‘敍;魅姐 1孩觸媒成份換算成Ti為0.28毫萁耳、三乙 基紹80奄莫耳、和觸媒第S成份的二異丙基二甲氧基矽 烷8牽莫耳組合而成的誨媒對聚合器供應丙烯和乙烯 的混合氣髖之前.將氣〇K j’盼5(&gt;·5骜耳充填入聚合器内,接著 不將未反應混合氣體排出A „ 出聚合器外,而Μ可保持聚合屋 力0.69HPa的供應速度,對聚合器供應丙烯93 4莫耳χ 和乙烯6.6莫耳X組成的绲合氣賭且聚合溫度為6〇1〇 ,餘按實施例1同樣處理,製造丙稀-乙稀共聚物,得 比較例1評估試樣。 fch 龄 Μ 2 使用外消旋乙铺雙(節基)二氯化給〇〇9毫奠耳和内消 旋乙嫌雙(節^)二氯化給〇.〇1奄莫耳之混合物,.做為二 實施例1同樣條件,實^丙烯-乙烯的共 的精製步驟◊從聚合器取出含共聚物之溶 共聚物全部溶於溶劑内,其後按實施例5 溶劑,投入甲酵,進行共聚物的析出、過 丙烯-乙烯共聚物,得比較例2評估試樣。 ⑵而锸-7,烯&amp;聚物的物裨銶仕 络金羼,餘按 聚合和共聚物 劑部份時,因 同樣減壓餾去 漶、乾燥,得 -21- 本紙張尺度適用中國國家樣率(CNS ) Α4规格(210X297公兼) (請先閲讀背面之注意事項再填寫本頁) 裝. 訂· A7 B7 五、發明説明(20 ) 就實施例1〜5和比較例1〜2所得各評估試樣,测 定下述物性。評估结果如表1所示。 (a) 全乙烯單元含量,利用ϋ(:核磁共振譜測定(單 位為萁耳χ )。 (b) 三價基分率(PEP):共聚物主鏈中三個單體鐽單 元(三價基),係「丙烯單元—乙烯單元◊丙烯單元」連 接分率,由13 C核磁共振譜測定。 (c) 三價基分率(EEE):共聚物主鯆中三個單體鐽單 元(三價基),係「乙烯單元乙烯單元4乙烯單元」連 接分率,由13 C-核磁共振譜测定。 (d) 相對於全丙烯單元含量(C3)的α, /3-亞甲碳數比 率(Να/3): GC核磁共振譜測定(單位為萁耳X )。 (e) 重量平均分子量(nW):由GPC測定。 (f) 數平均分子量(MrO:由GPC測定。 (g) 融點(Tb):由GPC測定(單位為1^)。 --c^— (請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局貝工消费合作社印製 -22- •Γ·. 本外張尺度適用中國國家揉準(〇阳)八4*1^(210父297公釐) A7 B7 五、發明説明(21 表1 實 施 例 比 較例 號 次 3 4 5 1 2 乙烯含量(莫耳Si ) 3.22 4.41 2.05 7,14 14.3 6.50 4.88 三價基分率(PEP) (Χίο2) 2.78 3.69 1.66 5.70 10.44 4.60 4.00 三價基分率(ΕΕΕ)(&gt;ί102 ) 0.00 0.06 0.00 0.12 0.34 0.40 0.06 〇(,/3-亞甲碳數比率1&lt;«/9(萁耳51!) 0.07 0.07 0.07 0.08 0.20 &lt;0.01 1.41 重量平均分子量(Mw)(xl04) 18.9 90.0 18.5 35.3 7.2 19.0 25.8 平均分子置比(Mw/Mn) 2.3 2.8 2.2 1.7 2.2 4.1 2.0 融點(Τβ)ΟΟ) 139.7 137.4 150.0 116.1 115.3 139.5 109.5 Γ t j\r --- - I (請先聞讀背面之注意事項再填寫本頁) • IL. @丙烯-7.慊共聚物成型品的射出成塑 於實施例1所得丙烯-乙烯共聚物100重量份,混合 四[亞甲-3-(3’,5’-二特丁基-4’-羥笨基)丙酸酯]甲烷 0.1重量份,和硬脂酸鈣0.1重量份。此混合物使用壓 出溫度設定在230C而螺桿徑40βιβ的單軸壓出製粒機壓 出,得共聚物顆粒。所得顆粒K射出成型機在熔態樹脂 溫度230t:,金觸模型溫度50t射出成型,製JIS形試 樣。 hh齩俐3 除使用比較例1所得丙烯-乙烯共聚物外,按實施例6 同樣條件處理,製成JIS形試樣。 (4·)成型品的耐熟神諫估 -23- 本紙張尺度適用中國圃家揉牟(CNS ) A4規格(210X297公釐) _訂 經濟部中央橾準局貝工消費合作社印製 A7 B7 五、發明説明(22 ) 將實施例6和比較例3製成的試樣,於相對濕度50¾ 、室溫23C的室内放置72小時後,根據JIS K 7207,在 45.1N/cm2的屈曲壓力下,测定扭曲溫度(HDT)(單位為 t:),評估酎热性。 實施例6和比較例3試樣的扭曲溫度(HDT),分別為 1011 和 gst: 〇 扭曲溫度(HDT)愈高,表好附熟性良好。 (5)丙锸-7.铺共费物_甲;甲 g嘸俐7, 1T 4 This paper is applicable to Chinese National Standard (CNS) Α4 standard (210 × 297 mm.). The Ministry of Interest and Economic Development Bureau of the Central Government Procurement Cooperation Du Yin *. A7 B7 V. Inventor Sun and Moon (l4) The catalyst of the above-mentioned combination of dioxofluorene and alumoxane, but the amount of each of the catalyst components is 10-1,000,000, compared with the transition gold atom of the dioxane, and the aluminum atom in the alumoxane is 10 ~ 1,000,000. More preferably, 50 to 50,000 moles are preferred, and 100 to 30,000 moles are particularly preferred. In the second gist of the present invention, in the presence of the catalyst obtained by the combination described above, propylene and ethylene can be copolymerized to prepare the propylene-ethylene copolymer of the first gist of the present invention, but the polymerization method can use a known propylene ( Co-polymerization process, for example, in aliphatic hydrocarbons such as butane, pentane, hexane, heptane, octane, cycloaliphatic hydrocarbons such as cyclopentane, hexane, methylcyclohexane, toluene, xylene, Aromatic hydrocarbons such as ethylbenzyl can be used in inert solvents such as gasoline fractions or gasoline tanks, and the slurry polymerization method of polymerizing propylene and ethylene, and using propylene itself as a solvent, the entire copolymerization with Μ, and Any gas phase copolymerization method in which the copolymerization of propylene and ethylene is performed in the gas phase may be used. In addition, the copolymerization can be carried out in a continuous ore type, a batch type or an f-batch type. In the copolymerization of propylene and ethylene, the above catalysts can be pre-mixed with two components of dioxofluorene and oxaloxane in an inert solvent, and then supplied to the copolymerization reaction. Dioxofluorene and alumoxane can also be separately supplied. To the copolymerization reaction 糸. In addition, before the copolymerization of propylene and ethylene, it is possible to react a small amount of α-olefins in the inert solvent of the catalyst of dioxometallurgy and aluminum oxide, specifically, each mole of dichromium The transition metal is used to make the α-olefin polymerize from about 0.001 to 10 kg. After the catalyst is preactivated, copolymerization of propylene and ethylene is carried out. Finally, good particles of propylene-ethylene copolymer are obtained, which is also effective. -16- This ¥ Zhang scale applies to China's national kneading rate (CNS) Α4 size (210X297 mm) '---- (Please read the note on the back before filling this page) £ Equipment_ Order Zhongji, Central Kneading A7 _ ._B7 ___ printed by the quasi-government industrial-consumer cooperation V. Description of the invention (15) Can be used for pre-activated 0C-olefins, including C2-12 Ot-olefins, specific examples include ethylene, propylene, butene, pentene Ene, hexene, octene, 4-methyl-1-pentene, etc., especially K ethylene, propylene, 4-methyl-1-pentene are preferred. In the second gist of the present invention, if the propylene and ethylene are copolymerized by using the pre-image method in the presence of a pre-activated catalyst, the same polymerization conditions as those commonly known as optically active rhenium catalysts for polymerizing propylene can be used as the copolymerization conditions. . That is, the polymerization degree is from -50 to 150t: JW-10 to 100P is preferred, the polymerization pressure is from atmospheric pressure to 7MPa, and K0.2 to 5MPa is preferred. The propylene and ethylene are supplied into the polymerizer, which is usually carried out for 1 minute to 20 hours. Left and right copolymerization. In addition, during the polymerization, similar to the conventional copolymerization method, an amount of hydrogen can be added to control the molecular weight. After the completion of the copolymerization of propylene and ethylene, if necessary, it may be subjected to post-treatment steps such as a known deactivation treatment step, a residue removal step, and a suspicion step to prepare a soft propylene-ethylene copolymer according to the first step of the present invention. In the method for producing a propylene-ethylene copolymer according to the second gist of the present invention, ethylene and propylene are copolymerized in the presence of a catalyst of a combination of a precursor dichromium metal and an alumoxane. In the insertion reaction, isopyrene hardly occurs. On the other hand, during the ethylene insertion reaction, the ore-sparing insertion reaction of ethylene is suppressed, and the ethylene units are more randomly incorporated in the copolymer. As a result, in the method for preparing a propylene-ethylene copolymer according to the second gist of the present invention, a monomer 鐽 which supports a more random combination of ethylene units, has a small amount of heterogeneous bond of propylene units, and has a narrow molecular weight analysis is the first gist of the present invention. -17- The paper Λ degree applies to the Chinese National Standard (CNS) A4 specification (210X297 cm) (Please read the note on the back before filling out this page) -s ^ _. Printed by the Consumer Cooperatives in the Central Bureau of the Ministry of Economic Affairs A7 _ _B7___ V. Propylene-ethylene copolymer of invention description (16). In the molded article of the third aspect of the present invention, the propylene-ethylene copolymer which is the first aspect of the present invention is optionally blended with an anti-gasification agent, an ultraviolet absorbent, an antistatic tritium, a nucleating agent, a detergent, Various additives such as flame retardants, anti-blocking tinctures, coloring «, filling of inorganic or organic materials, and various synthetic resins, in powder form, or using a melt blender at 190 ~ 35QeC, heating and mixing for 20 seconds to 30 About 0 minutes, and then cut into granules to form a granular state for molding materials. "The molding method can use various known polypropylene molding methods, such as injection molding, extrusion molding, foam molding, hollow molding, etc. Various industrial injection molding components, various containers, non-stretched film, uniaxially stretched film, biaxially stretched film, cast iron, tube, fiber, etc. can be made. Molded products β Sound stealing examples The present invention can be borrowed from examples and comparisons The example further details the β m propion sample-7, sample # & _ &gt; The equipment has a stainless steel mesh polymerizer with inclined blades and a stirrer with a content of 10 OdB3, which is purged with nitrogen. In the aggregator, at 20e C gi degree: n-hexane 50dn 3, methylaluminoxane toluene solution (product of Dongsu Aikesu Company, trade name MMA0, concentration 2id (d · 3), converted to aluminum atom is 2.0 · 〇1, and optical rotation Methylsilylidene (2,3,5-trimethylchenpentadienyl) (2 ·, 4 ·, 5'-trimethylfluorpentadienyl) dicyanide 0.09 mmol and Racemic Dimethyl Silane (2,3,5- -1 8-(Please read the note on the back and write this page first) 〉 A4 specification (210X297 mm) A7 B7 V. Description of the invention (17) Trimethylcyclopentadienyl (2,3,5, -trimethylpyridylcyclopentadienyl) digasified to 0.01 milliliter The mixture of Moore was used as dioxin, together with toluene 0.5 da 3 〇 Then, after the temperature in the polymerizer was raised to 45 υ, the content of propylene was 93.9 mol χ, ethylene 6.0 mol χ and hydrogen oi mol χ. The mixed gas is supplied to the polymerizer at a supply speed of 8dm3 / rain, and the temperature in the polymerizer is maintained at 451C. A part of the mixed gas in the gas phase part of the polymerizer is installed in the polymerizer separately. Phase valve Out of the polymerizer, M kept the pressure at 0.4M Pa, and co-polymerized C and C for 4 hours. Employees' cooperatives of the Central Bureau of Standards, Ministry of Economic Affairs, the consumer co-operatives (please read the precautions on the back before filling out this page) Polymerization After the reaction is completed, unreacted propylene and ethylene are released from the polymerizer, and 2-propanol 3dm 3 is put into the polymerizer, and the catalyst is deactivated at 30t: stirring for 10 minutes. Aeration is added. Aqueous hydrogen solution (concentration: 12ind / dm3 &gt; 0.2dm3 and formazan 8dm3) was treated at 60¾ for 30 minutes. After the treatment is completed, stop stirring, remove the aqueous phase from the bottom of the polymerizer, add the same amount of hydrogen chloride aqueous solution and formazan, and repeat the same operation. Next, add an aqueous solution of sodium hydroxide (concentration: 5.11〇 丨 / € || 113) 0.02 (1113, water 2 &lt; 1 || 13 and methanol 2dm3, and stir for 30 minutes at 30¾. After the treatment, stop the stirring from After removing the water phase part under the polymerizer, add 8dm3 of water again, at 30 t: stirring treatment for 10 minutes, the operation of removing the water phase part is repeated twice, and the polymer slurry is taken out from the polymerizer, dried and dried to obtain A propylene-ethylene copolymer of 2.4 kg was used as the evaluation sample of Example 1. When Pali 2 changed the n-hexane used in Example 1 to toluene 50dm 3 as the polymerization solvent-19. (CNS) A4 specification (210X297 mm) A7 B7 V. Description of the invention (18), the mixed gas component supplied to the polymerizer is propylene 90. 5 mol ", 9.5 mol ethylene, hydrogen / 0, polymerization temperature The temperature is 30C, and the rest is made under the same conditions as in Cell Example 1. A propylene-ethylene copolymer was produced to obtain an evaluation sample of Example 2. —Li Li 3 The composition of the mixed gas supplied to the polymerizer was: propylene 96.8 Moore X, ethylene 3.2 箕 S:, · Hydrogen 0, and polymerization temperature 50 * 0, and the rest were made under the same conditions as in Example 1. A propylene-ethylene copolymer was obtained in Example 3. g 敝 Example 4 The n-hexane used in Example 1 was changed to 50dm3 of toluene as the polymerization solvent, and the composition of the mixed gas supplied to the polymerizer was propylene 84.8. Moore !, ethylene, 15.1 mole V, and hydrogen 0.1 mole. I used the same conditions as in Example 1 to produce a propylene-ethylene copolymer. Example 4 Evaluation Sample 6 was obtained. Printed by Industrial and Commercial Cooperatives (please read the precautions on the back before filling out this page) Use dimethylsilane (2,3,5-trimethylcyclopentadienyl) (2 ', 4!, 5 '-Trimethylcyclopentadienyl) chromium dichloride 0.09 mmol and dimethylsilylidene (2,3,5-trimethylcyclopentadienyl) (2', 3 ', 5 '-Trimethylcyclopentadienyl) dichloride mixture with 0.01 millimolars, as the diluentine, and the mixed gas supplied to the polymerizer becomes propylene 91.1 mol S; ethylene 8.8 Ear S; Hydrogen 0.1 and Ear 3J. After performing propylene-ethylene copolymerization and copolymer purification under the same conditions as in Example 4 of the cell, the solvent portion containing the copolymer was taken out from the polymerizer. • The 珉 standard is applicable to China's National Standards (CNS) M specifications (210X297 cm) /.· V. Description of the invention (19 A7 B7) The copolymer is dissolved in the solvent removed from the printed materials of the Central Government Bureau of the Ministry of Economy All, this solution is put into the solvent depressurization age removal device, and under jg · η;-. '® 701: After distilling off 95¾ methylbenzyl, and cooling to 25¾ .. Put in a manurease to put 3'_ The copolymer was taken out, dried, and dried to produce a propylene-ethylene copolymer. Example 5 Evaluation Sample 0 fch »Li 1 The catalyst used in Example 1 was used as a catalyst (~ chromium metal and methylalumoxane). The chlorinated continuum-bearing type was used instead; the catalyst component of Meijie 1 was converted to Ti with 0.28 millitorr, triethyl sulphate 80 mol, and the diisopropyl dimethoxide of the S component of the catalyst. Before the polymer mixed with silane and 8 moles is supplied to the polymerizer, a mixed gas of propylene and ethylene is supplied to the polymerizer. Fill the polymerizer with gas 〇K j 'hope 5 (&gt; The reaction mixture gas is discharged out of the polymerizer, and M can maintain a supply rate of 0.69 HPa for the polymerization room power, and supply 934 to the polymerizer. Gun alkenyl 6.6 X molar composition of the gas bet engagement and the polymerization temperature was 6〇1〇, than the same process as in Example 1, producing propylene - ethylene copolymer, Comparative Example 1 to obtain evaluation samples. fch age M 2 uses a mixture of racemic ethidium bis (syl) dichloride to give 009 millimoles and meso ethyl bis (syl) dichloride to 0.001 mol, As the same conditions as in Example 1, the propylene-ethylene co-refining step was carried out. The copolymer-containing soluble copolymer was taken out of the polymerizer and dissolved in the solvent. Then, the solvent of Example 5 was added to the formic acid. The copolymer was precipitated and the propylene-ethylene copolymer was obtained to obtain a comparative example 2 evaluation sample. ⑵ and 锸 -7, ene &amp; polymer properties of Shiluo Jinyao, the rest of the polymerization and copolymer agent parts, because the same distillation under reduced pressure and drying, -21- This paper size applies to China National Sample Rate (CNS) Α4 specification (210X297), (please read the precautions on the back before filling out this page) Binding. Order · A7 B7 V. Description of the invention (20) For Examples 1 to 5 and Comparative Example 1 to Each of the obtained evaluation samples was measured for the following physical properties. The evaluation results are shown in Table 1. (a) Total ethylene unit content, measured by ϋ (: nuclear magnetic resonance spectroscopy (unit: χ χ). (b) Trivalent fraction (PEP): three monomer fluorene units (trivalent in the main chain of the copolymer) Base), which is the connection fraction of "propylene unit-ethylene unit / propylene unit", determined by 13 C nuclear magnetic resonance spectroscopy. (C) Trivalent radical fraction (EEE): Three monomer units of the main unit of the copolymer. Trivalent group), which is the connection fraction of "ethylene units, ethylene units, 4 ethylene units," determined by 13 C-NMR spectrum. (D) α, / 3-methylene carbon number relative to the total propylene unit content (C3) Ratio (Nα / 3): GC Nuclear Magnetic Resonance Spectroscopy (Unit: Xerox). (E) Weight average molecular weight (nW): measured by GPC. (F) Number average molecular weight (MrO: measured by GPC. (G) Melting point (Tb): Measured by GPC (unit is 1 ^). --C ^ — (Please read the notes on the back before filling this page) Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs-22- • Γ ·. This scale is applicable to the Chinese national standard (0 Yang) 8 4 * 1 ^ (210 father 297 mm) A7 B7 V. Description of the invention (21 Table 1 Example Comparative Example No. 3 4 5 1 2 Ethylene content (Molar Si) 3.22 4.41 2.05 7,14 14.3 6.50 4.88 Trivalent base fraction (PEP) (Χίο2) 2.78 3.69 1.66 5.70 10.44 4.60 4.00 Trivalent base fraction (ΕΕΕ) (&gt; (102) 0.00 0.06 0.00 0.12 0.34 0.40 0.06 〇 (, / 3-methylene carbon number ratio 1 &lt; «/ 9 (萁 耳 51!) 0.07 0.07 0.07 0.08 0.20 &lt; 0.01 1.41 weight average molecular weight (Mw) (xl04) 18.9 90.0 18.5 35.3 7.2 19.0 25.8 Mean molecular ratio (Mw / Mn) 2.3 2.8 2.2 1.7 2.2 4.1 2.0 Melting point (Tβ) 〇) 139.7 137.4 150.0 116.1 115.3 139.5 109.5 Γ tj \ r ----I (Please read first Note on the back, please fill in this page again) • Injection molding of IL. @ Propylene-7. 慊 copolymer molded product in 100 parts by weight of the propylene-ethylene copolymer obtained in Example 1, mixed with four [Methylene-3- (3 ', 5'-Di-tert-butyl-4'-hydroxybenzyl) propionate] 0.1 part by weight of methane, and 0.1 part by weight of calcium stearate. This mixture uses a single unit with an extrusion temperature set at 230C and a screw diameter of 40βιβ. Coaxial pellets were pressed out to obtain copolymer pellets. The obtained pellet K injection molding machine was injection molded at a molten resin temperature of 230t :, and a gold contact mold temperature of 50t to prepare a JIS-shaped test sample. hh 齩 利 3 Except using the propylene-ethylene copolymer obtained in Comparative Example 1, the same conditions as in Example 6 were used to prepare a JIS-shaped sample. (4 ·) Estimated maturity resistance of molded products-23- This paper size is applicable to the Chinese garden family (CNS) A4 specification (210X297 mm) _ Order printed by the Central Labor Bureau of the Ministry of Economic Affairs and printed by the Shellfish Consumer Cooperatives A7 B7 V. Description of the invention (22) After the samples prepared in Example 6 and Comparative Example 3 were placed in a room with a relative humidity of 50¾ and a room temperature of 23C for 72 hours, according to JIS K 7207, at a flexural pressure of 45.1 N / cm2 , Measure the twist temperature (HDT) (unit is t :), and evaluate the heat resistance. The distortion temperature (HDT) of the samples of Example 6 and Comparative Example 3 were 1011 and gst, respectively: 〇 The higher the distortion temperature (HDT), the better the surface and the maturity. (5) 丙 锸 -7. Shop common expenses_ 甲 ; 甲 g 呒 莉 7

於實嫌例1所得丙烯-乙鋪共聚物1〇〇重量份,混合 三(2,4-二特丁基苯基)隣酸酿〇.1重量份,四[亞甲ΐ-Ο',5'-二 特丁基 -4’-羥苯基 ) 丙 酸酯]甲烷 〇.〇5 重 量份, 和硬脂酸鈣0.0 8重量份。此混合物以設定壓出溫度230C 而螺桿徑40ββ的單抽壓出製粒機壓出,得共聚物粒。所 得顆粒在熔化壓出溫度210Ρ,冷卻輥溫度30t:,和線 速度20m/*in的條件,利用T模法製成厚25w 1、寬300ιβιβ 的膜。 fch齡俐A 經濟部中央橾準局貝工消費合作杜印製 (請先閲讀背面之注意事項再填寫本買) 除使用比較例1所得丙烯-乙烯共聚物外,按實施例 7同一條件處理,利用T模法製成厚25 wm,寬30010·^ 膜。 尚篇的辣仕訨除 躭實施例7和比較例4製成的膜,利用下述方法,測 定熱封溫度和揚氏係数(縦向·· MD,横向:TD)。 &quot;24- 本产張尺度適用中國國家橾準(CNS ) A4规格(210X297公釐)' 五、發明説明(25 ) Α7 Β7 經濟部中央揉率局貝工消费合作社印裂 (a) 热封溫度:取膜,利用熱傾斜式密封溫度测定機 (東洋精機公司製品),在密封壓力0.098MPa,密封時間 1秒的條件下,進行熱封。其次,將熱封的膜切醑成寬 15mm,使熱封部在中央,於拉速300*m/iiin條件下,進 行抗拉試驗,Μ斷裂時的應力為膜的熱封強度,測定热 封強度達0.0271^8/15«11»時所需熱封溫度(簞位為^!)。 (b) 楊氐係數:根據ASTM D 882测定MD(縱商)TD(横 向)的抗拉強度(單位為N/bib2 )。 實施例7和比較例4製成膜的熱封溫度和楊氏係數測 定結果如下。 表2 楊氏係數 熱封溫度) HD(縦1¾ ) TD(横向) 實胞例7 135 550 比較例4 141 530 熱封溫度低者,從節省能源觀點言 有利,楊氏係數愈高,翊性愈大。 链明物里 本發明丙烯-乙烯共聚物,如實施例的表1所示,幾 無丙烯插入,反應引起的異種鍵存在,乙烯單元更加無規 结合,且分子董分佈狹。结果,Μ本發明丙烯-乙_共 聚物為成型材料之成型品,與使用鈦觸媒,而融點與習 知技術所製造相同的丙烯-乙烯共聚物成型品相較,射 出成型品具有良好耐热性,膜具有良好剛性和優良低溫 -25- 560 540 在工業性生產上 (請先Μ讀背面之注項再填寫本頁) —*^4^.. 訂 本紙張尺度適用+國國家揉準(CNS ) Α4规格(210X297公釐) A7 B7 五、發明説明(24 ) 熱封性,可廣用於習知丙烯-乙烯共聚物受限的用途。 匾忒簡屋說明 第1圖為實施例1所得本發明丙烯-乙烯共聚物的13 C 核磁共振譜。、 第2圖為本發明丙烯-乙烯共聚物製法滾程圖。 &gt; 「 —J--·*&quot;^-- (請先閲讀背面之注意事項再填寫本頁) ΟIn 100 parts by weight of the propylene-ethylenic copolymer obtained in Example 1, 0.1 parts by weight of tris (2,4-di-tert-butylphenyl) o-acid was mixed, and tetrakis [methylenefluorene-O ', 5'-di-tert-butyl-4'-hydroxyphenyl) propionate] 0.05 parts by weight of methane, and 0.08 parts by weight of calcium stearate. This mixture was extruded in a single extraction granulator with a set extrusion temperature of 230C and a screw diameter of 40ββ to obtain copolymer pellets. The obtained pellets were melted and extruded at a temperature of 210 P, a cooling roller temperature of 30 t :, and a linear velocity of 20 m / * in, and a T-die method was used to form a film having a thickness of 25 w 1 and a width of 300 μm β. fch Ling LiA Printed by Shellfish Consumer Cooperation Department of the Central Bureau of Standards and Quarantine of the Ministry of Economic Affairs (please read the notes on the back before filling in this purchase) Except using the propylene-ethylene copolymer obtained in Comparative Example 1, use the same conditions as in Example 7 , T-die method was used to make a film with a thickness of 25 wm and a width of 30010 · ^. Existing spicy recipes: The films made in Example 7 and Comparative Example 4 were measured, and the heat-sealing temperature and Young's coefficient were measured by the following methods (direction: MD, transverse direction: TD). &quot; 24- The production scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 'V. Description of the invention (25) Α7 Β7 Printed by the Central Labor Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative (a) Heat seal Temperature: The film was taken out and heat-sealed using a heat-inclined sealing temperature measuring machine (manufactured by Toyo Seiki Co., Ltd.) under the conditions of a sealing pressure of 0.098 MPa and a sealing time of 1 second. Next, the heat-sealed film was cut to a width of 15 mm, with the heat-sealed portion in the center, and subjected to a tensile test at a tensile speed of 300 * m / iiin. The stress at M fracture was the heat-sealing strength of the film, and the heat was measured. The heat seal temperature required when the seal strength reaches 0.0271 ^ 8/15 «11» (the position is ^!). (b) Young's coefficient: The tensile strength of MD (vertical quotient) and TD (horizontal) is measured according to ASTM D 882 (unit is N / bib2). The results of measuring the heat-sealing temperature and Young's coefficient of the films made in Example 7 and Comparative Example 4 are as follows. Table 2 Young's coefficient heat-seal temperature) HD (縦 1¾) TD (transverse) Cell example 7 135 550 Comparative example 4 141 530 The lower heat-seal temperature is advantageous from the viewpoint of energy saving, the higher the Young's coefficient, the better Bigger. As shown in Table 1 of the examples, the propylene-ethylene copolymer of the present invention has almost no propylene insertion, heterogeneous bonds caused by the reaction, ethylene units are more randomly bound, and the molecular distribution is narrow. As a result, the propylene-ethylene copolymer of the present invention is a molded product of a molding material. Compared with a propylene-ethylene copolymer molded product manufactured using a conventional technology and having a melting point similar to that of a conventional technology, the injection molded product has a good performance. Heat resistance, film has good rigidity and excellent low temperature -25- 560 540 For industrial production (please read the note on the back before filling out this page) — * ^ 4 ^ .. The paper size is applicable to the country + country CNS A4 Specification (210X297mm) A7 B7 V. Description of the Invention (24) Heat-sealability can be widely used for the limited use of propylene-ethylene copolymers. Explanation of plaques and simple houses Figure 1 is a 13 C nuclear magnetic resonance spectrum of the propylene-ethylene copolymer of the present invention obtained in Example 1. Figure 2 is a rolling diagram of the propylene-ethylene copolymer manufacturing method of the present invention. &gt; "—J-- · * &quot; ^-(Please read the notes on the back before filling in this page) Ο

C 經濟部中央標準局貝工消費合作社印裝 -26- 本p尺度適用中國國家標準(CNS ) Μ说格(210X297公釐)C. Printed by Shellfish Consumer Cooperatives, Central Bureau of Standards, Ministry of Economic Affairs -26- This p-scale applies Chinese National Standards (CNS)

Claims (1)

經濟部中央標準局員工消費合作社印褽 7T、申請專利祀.圍 1. 一種丙烯-乙烯共聚物,包括0.01〜15莫耳X乙烯單 元和99.99〜85莫耳S;丙稀單元,其特徵為: U)由核磁共振譜-的鐽構造為: (a-1)在共聚物主鏈的三假單賭鍵單元價基)欠 ,丙烯單元-乙烯單元-丙烯單元相連的分率(MP)與 全乙烯單元含量(C2)間,呈式(I)闞係: 0.0070X C2-0.002 P E P 赛 0 · 0 07 0 X C.2 + 0 . 0 1 3 0 ( I ) (a-2)在共聚物主鏈的3涸單頻鐽-單元(三價基)Φ ,三個乙烯簞元相連的分-皐(EEE)與S烯嚴-¾總含量、 r (C2&gt;間,圼式(m闞係: Ο ^ E E E ^ 0.00 0 3 3 X C2 10 ( I ) U-3)相對於全丙烯單元的α,/3-亞甲基總碳數的 tfc率(Η α /?),在0〜1 . 2莫耳3!範圍, (b) 重暈平·均分子量(Mvl為50, 000〜1,500,000, &amp; - (c) 重量平均分子量(My對數平均分子量(Μη)之比 Uw/Hn)為 1 . 2〜3 . 8者。 2, 如申請專利範圃第1項之丙烯-乙烯共聚物,其中共一 聚物的融點(;Tm)與全乙嫌Ji元含悬(C2)間,具有式 (I ): -8 . 1 X G 2 + 1 5 6.0 S Τι ^ -4.4 x C 2 + 16 5. 0 ( II I 所示闞係者。 3. —種丙烯-乙嫌共聚物之製法,該丙烯-乙烯共聚物, 包括0.01〜15奠耳S:乙烯單元和9 9.99〜85莫耳J;丙 ’-27- 本紙張尺度逋用中®國家標準(CNS &gt; Α4规格(210X297公釐) n I I HI V Μ· - V —l·* n (請先閲讀背面之注項再填寫本頁) .、1T' A8 B8 C8 D8 387919 六、申請專利範圍 鋪單元,其中: (a) 由核磁共振譜的鍵搆造為: U-1 )在共聚物主鐽的三傲單,體鏈里 ,丙烯-元-乙1里i二既麗單元桓麗放 全乙蓋星_元含量(C 2)間,虽式(I )闞係 0 . 0070 X C2-0 . 0020 ^ PEF ^ 0.0070 x_ U-2)在共聚物主鐽的三個單體鏈單 ,三涸乙烯單元祖建的分率(EEE)與乙 (C2)間,呈式(H )闞係: 0 S EE ES 0,0003 3 x G2 +0.0410 (a - 3 )枏對於全®烯單元的《 , /3 -亞 比率(H e(尽),在0〜1 . 2冥-4 X範圍, (b) 簠量平均分子量(MW)為50,0.00〜 :―且: (c) 重董平均分子量(M*&gt;對數平均分 心Mw/Mrt)為 1.2〜3·δ, 其特徵為,在通式(0所示旋光性過渡金 嫫檢败遽的應JT存在下,將乙稀和丙稀 元ί三價基)中 分率(PEP)與 ♦ C2 + 0.013H I ) 元(三價基)中 烯單元總含量 甲羞總碳數的 1,500,000, 子量(Μη)之比 屬化合物和紹 予Μ共聚合:. (請先閲讀背面之注$項再填寫本頁) 經濟部中央標準局貝工消費合作社印II /(C«-aR *β) \ / Q Μ Ns(C.H«.nR,n)/ X X Y (1) 式中,M為選自妹、锆和給的《波金鼷原子,X和Y 相闻或不同,為氫原子、鹵素原子或烀基,(C5 H4,,m Pm ) 和(c5H4-n R2n &gt;净被取代環戊二烯基,其中R 1和R 2 28 +纸張尺度逋用中國國家揉·串(CNS &gt;A4規格(210X297公釐) 經濟部中央橾準局貝工消費合作社印製 3*7919 Μ C8 D8 六、申請專利範園/ 相同或不同,為C 1 - 20烴基,可與環戊二輝的環上 二個碳原子结合形成—W上的煙環,亦可Μ烴基取代 ,或為含砂烴基,m和η為1〜3整數,Q為選自烴基 、未被甲砂烷叉基-和烴取dt甲矽烷叉基,可將-(¾ HuR1# )和C% R2n )交聯之二價基者。 4.如申請專利範圍第3項之丙烯-乙烯共聚物之製法, 〜其中旋秦搜過1金爵俗合—擻係通式⑴^ 子,X和Υ相同或不同,為鹵素原子或經基,R1和 R 2相同或不同,為C 1 - . 2〇烷基,而Q為二烷基甲矽 烷叉基者。 5 . —種成型是*其首徵為Μ下逑丙烯-乙爲共聚物為成 型材料成型,該丙-燒-乙炼共聚物择括〇.〇1〜I5莫耳r 乙烯里和—9 9 · 9 9〜8 5奠耳X丙烯單元•其中: 丄 U )由-梭磁,其振譜的鐽構造為: U-1)在共聚物主鍵的三偃畢通鏈單元(三價基)中 ...·' . ..... . . . - ,丙烯單元-乙嫌單元-丙嫌單元相連的分率(PEP)與^ 全乙JMT元含量(&amp;幻間,圼式(I )闞係: 0 . 0 0 70 x02-0.0 020^ PEP^ 0.0070 xC2 + 0.013 0(I) (a-2)在共聚物主鍵的三涸單酱鍵單元(三價基)中 三個乙烯單元相連的分率(EEEK與乙輝單元縷含量 . (C2,間,呈式(I ) 81係: 0 容 ΕΕΕέ 0.00033 X C2 + 0.0010 (1} (a-3)-相爵於全丙烯單元的a , -亞甲基總碳數的 比率(Ν α /3 ),在0〜1.2莫耳X範圄, -29- 本紙張尺度逋用中國两家標!M CNS &gt; Α4软潘(210X297公釐} HI i^i^— nn —It JMme— n (請先閲讀背面之注^^項再填寫本頁) i11 _Γ A8 D8 六、申請專利範圍 (b)重量平均分子量(fhf)為50, 000〜1, 500,000, r&quot; ^ . . 且 (C)重量平均分子量(Mw)對數平均分子量(Μη)之比 Uw/Mn j 為 1 . 2〜3.8者。 6. 如申請專利範圍第5項之成型品,係由丙烯-乙烯共 珐物射出成型者。. 7. 如申請專利範圍第5項之成型品,係由丙歸-乙烯共 聚物壓卑成型者。 8C如申請專利範圍第5項之成型品,該成型品為薄膜者。 聚物射出成型者。 (請先閲讀背面之注^^項再填寫本頁) 裝.— 訂------^ 經濟部中央梂準局貝工消費合作社印裝 -30- 夫紙張尺度適用中國國家標準(CNS ) A4規格(210X297公嫠)Employees' cooperative of the Central Standards Bureau of the Ministry of Economic Affairs of the People's Republic of China, 7T, applied for patents. Wai 1. A propylene-ethylene copolymer, including 0.01 to 15 Moore X ethylene units and 99.99 to 85 Moore S; acrylic units, which are characterized by: : U) The structure of 鐽 from the nuclear magnetic resonance spectrum is: (a-1) the three pseudo-single bond unit valence groups in the main chain of the copolymer) are owing, and the propylene unit-ethylene unit-propylene unit connection ratio (MP) With the total ethylene unit content (C2), the formula (I) is: (1) 0.0070X C2-0.002 PEP match 0 · 0 07 0 X C.2 + 0. 0 1 3 0 (I) (a-2) in The 3 涸 single-frequency 鐽 -unit (trivalent radical) Φ of the main chain of the copolymer, the total content of 皋 -E (EEE) and S-ene, which are connected to three ethylene units, the total content of r (C2 &gt; m 阚 series: 〇 ^ EEE ^ 0.00 0 3 3 X C2 10 (I) U-3) tfc ratio (, α /?) with respect to the total number of α, / 3-methylene carbons of all propylene units, in 0 ~ 1.2 Molar 3! Range, (b) weight halo · average molecular weight (Mvl is 50,000 ~ 1,500,000, &amp;-(c) weight average molecular weight (My log average molecular weight (Μη) ratio Uw / Hn) is 1.2 to 3.8. 2, such as the first item of the patent application park A propylene-ethylene copolymer in which the melting point (; Tm) of the co-polymer is between Ji and Yuan (C2), and has the formula (I): -8. 1 XG 2 + 1 5 6.0 S T ^ -4.4 x C 2 + 16 5. 0 (The system shown in II I. 3. A method for preparing propylene-ethylene copolymer, the propylene-ethylene copolymer, including 0.01 ~ 15 Moore S: ethylene unit and 9 9.99 ~ 85 Mol J; C'-27- This paper size is in use ® National Standard (CNS &gt; Α4 size (210X297 mm) n II HI V Μ ·-V —l · * n (Please read first (Notes on the back page are to be completed on this page). 1T 'A8 B8 C8 D8 387919 VI. Patent application range paving unit, where: (a) The bond structure of the nuclear magnetic resonance spectrum is: U-1) The three proud singles, in the body chain, the propylene-yuan-yi 1 li i two Li unit unit Li Li put full Biga star_yuan content (C 2), although the formula (I) is 0. 0070 X C2- 0. 0020 ^ PEF ^ 0.0070 x_ U-2) Between the three monomer chains of the main copolymer of the copolymer, the fraction of the ethylene unit ancestors (EEE) of the three units (EEE) and B (C2), the formula (H) 阚Series: 0 S EE ES 0,0003 3 x G2 +0.0410 (a-3) , / 3 -sub-ratio (H e (exhaust), in the range of 0 to 1.2 to 4 -4, (b) the weight average molecular weight (MW) is 50, 0.00 to:-and: (c) heavy average The molecular weight (M * &gt; log-average distraction Mw / Mrt) is 1.2 ~ 3 · δ, which is characterized in that in the presence of JT, which is an optically active transition metal represented by the formula (0), the ethylene and The ratio of propylene trivalent radical (PEP) to ♦ C2 + 0.013HI) yuan (trivalent radical) total olefin unit content of methyl ethyl, total carbon number 1,500,000, the ratio (Mη) of the compound and Shao Yu Co-polymerization: (Please read the note on the back before filling in this page) Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs II / (C «-aR * β) \ / Q Μ Ns (CH«. nR, n) / XXY (1) In the formula, M is selected from the group consisting of sister, zirconium, and zirconium. The X and Y atoms are different or different, and are hydrogen, halogen, or fluorenyl. (C5 H4, , m Pm) and (c5H4-n R2n &gt; net substituted cyclopentadienyl, in which R 1 and R 2 28 + paper size are used in Chinese national kneading and stringing (CNS &gt; A4 specification (210X297 mm) 3 * 7919 Μ C8 D8 printed by the Shellfish Consumer Cooperative of the Central Bureau of Standards, Ministry of Economic Affairs 6. Patent application park / Same or different, is C 1-20 hydrocarbon group, which can be combined with two carbon atoms on the ring of cyclopentadiene to form a smoke ring on W, which can also be substituted by M hydrocarbon group, or it contains sand. Hydrocarbyl, m and η are integers from 1 to 3, Q is selected from hydrocarbyl, non-methsaldinyl- and dt silylidene, and-(¾ HuR1 #) and C% R2n) can be cross-linked. Bivalent base. 4. If the propylene-ethylene copolymer is manufactured according to item 3 of the scope of application for patents, ~ Xin Qin has searched for 1 Jin Jue custom— 合 is the general formula ⑴ ^, X and Υ are the same or different, are halogen atoms or R1 and R2 are the same or different, and are C 1-.2 alkyl, and Q is dialkylsilylidene. 5. A kind of molding is * its first characteristic is M 逑 propylene-B is a copolymer for the molding material molding, the propylene-fired-acetic copolymer is optional 0.001 ~ I5 mole r ethylene and -9 9 · 9 9 ~ 8 5 Moore X propylene unit • Among them: 丄 U) by -Shu magnetic, the 鐽 structure of its vibration spectrum is: U-1) in the tripyridine unit (trivalent base) of the main bond of the copolymer ... · '. .......--, The fraction (PEP) of the connection of the propylene unit-the B unit-the C unit and the ^ full B JMT element content (&amp; magic, the formula (I ) Actinide: 0. 0 0 70 x02-0.0 020 ^ PEP ^ 0.0070 xC2 + 0.013 0 (I) (a-2) Three ethylene units in the triple-single-single-bond unit (trivalent base) of the primary bond of the copolymer Connected fractions (EEEK and Yihui unit content. (C2, between, formula (I) 81 series: 0 容 ΕΕΕέ 0.00033 X C2 + 0.0010 (1) (a-3) -phase of all acrylic units a,-the ratio of the total carbon number of methylene (N α / 3), in the range of 0 to 1.2 mole X range, -29- this paper size uses two Chinese standards! M CNS &gt; Α4soft pan (210X297 Mm} HI i ^ i ^ — nn —It JMme— n (Please read the note ^^ on the back before filling this page) i11 _Γ A8 D8 VI. Patent application scope (b) Weight average molecular weight (fhf) is 50,000 ~ 1,500,000, r &quot; ^.. And (C) Ratio of weight average molecular weight (Mw) to log average molecular weight (Μη) Uw / Mn j is 1.2 to 3.8. 6. If the molded article in the scope of the patent application is No. 5, the injection molding is made of propylene-ethylene co-enamel. 7. If the molded article in the scope of the patent application is No. 5, Those who are crushed and molded by acrylic-ethylene copolymer. 8C If the molded product of item 5 of the patent application, the molded product is a film. Polymer injection molded. (Please read the note ^^ on the back before filling (This page) Packing. — Order ------ ^ Printed by the Shellfish Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs. -30-Paper paper size is applicable to China National Standard (CNS) A4 (210X297 cm).
TW86100102A 1995-10-20 1997-01-07 Propylene-ethylene copolymer, preparation thereof and molding thereof TW387919B (en)

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JPH10298824A (en) * 1997-04-22 1998-11-10 Chisso Corp Fiber and fibrous formed product using the same
WO1999007747A1 (en) * 1997-08-12 1999-02-18 Chisso Corporation Process for the preparation of olefin (co)polymers, olefin copolymers, and application thereof
TW482770B (en) * 1997-08-15 2002-04-11 Chisso Corp Propylene/ethylene random copolymer, molding material, and molded article
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TWI247756B (en) 2003-08-22 2006-01-21 Mitsui Chemicals Inc Propylene random copolymers, use thereof and manufacturing method of the same
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