TW424100B - Polymerisation catalyst - Google Patents
Polymerisation catalyst Download PDFInfo
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- TW424100B TW424100B TW86113216A TW86113216A TW424100B TW 424100 B TW424100 B TW 424100B TW 86113216 A TW86113216 A TW 86113216A TW 86113216 A TW86113216 A TW 86113216A TW 424100 B TW424100 B TW 424100B
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F17/00—Metallocenes
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/619—Component covered by group C08F4/60 containing a transition metal-carbon bond
- C08F4/61908—Component covered by group C08F4/60 containing a transition metal-carbon bond in combination with an ionising compound other than alumoxane, e.g. (C6F5)4B-X+
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/619—Component covered by group C08F4/60 containing a transition metal-carbon bond
- C08F4/61912—Component covered by group C08F4/60 containing a transition metal-carbon bond in combination with an organoaluminium compound
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Abstract
Description
經濟部中夬標準局負工消費合作社印製 4 2 4 1 η ί Α7 _______Β7_ 五、發明説明(1 ) 本發明係關於某新穎性不連續金屬錯合物,其製法及 其當做適用於聚合烯烴之觸媒組成物的用途。尤其本發 明係關於包括一不連續錯合物及活性劑的觸媒組成物。 用過渡金屬來聚合1-烯烴(柄如乙烯)的用途在先前技 術裡係為已知。使用藉由以有機金屬化合物(例如三乙基 铭)活化鹵化鈦製得的Ziegler-Nattta觸媒對於許多製造聚 稀煙的商業方法而言是基本的。近二十或三十年來,進一 步的技術已經發展出具有如此高活性以致於含有非常低剩 餘物濃度之烯烴聚合物及共聚物可以直接以商業方法製得 的。存留在製得聚合物裡的剩餘觸媒數量是如此的小,以 致於對大部分商業用途而言不必要將分離及去除。如此的 方法可以藉由在氣相中聚合單體,或在烴類稀釋液的溶液 或懸浮液中操作。單體可以在氣相中(“氣相法,,>,例如藉 由在聚合條件下使用包括氣態單體的流體化氣體物流使包 括目標聚烯烴粉末及所要觸媒顆粒的床流體化來進行聚合 。在所謂的《溶液方法”中,(共)聚合反應係在使所得聚烯 烴形成烴類稀釋溶液的溫度及壓力條件下將單體導入烴類 稀釋液中觸媒溶液或懸浮液來進行》在“泥漿方法”中,選 擇溫度,壓力及豨釋液,使得所得的聚烯烴形成烴類稀釋 懸浮液。這些方法通常以相當低的壓力(例如10-50巴)及 低溫(例如5〇-15〇。〇操作。 商業製造各種不同種類及等級的商用聚乙烯。使用以 過渡金屬為底質的觸媒進行乙烯的高聚合反應,製得所謂 的‘‘高密度,,等級的聚乙烯《這些聚合物具有相當高的硬度 (請先閱讀背面之注意事項再填寫本頁) -裝·- 訂 線 J— 本紙張尺度適用中國國家標率(CNS ) a4規格(210 X 297公釐) 4 424100 , 424100 , 經濟部中央橾準局貝工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) Α4規格(2ΙΟΧ2?7公釐) A7 B7 五、發明説明(2 ) " 並可用來製造需要固有剛性的物件β商業上使用己稀與高 碳數1-稀烴(例如丁稀,己稀或辛稀)的共聚合反應,得到 各種各樣密度不同且其其它重要物理性質不同的共聚物。 使用以過渡金屬為底質的觸媒進行乙烯與高碳數卜烯烴共 聚合而得的特別重要共聚物係為具有密度0 91 0 93的共聚 物。這些通常在此項技藝裡稱為“線性低密度聚乙烯,,的共 聚物在許多方面都類似由乙烯進行高壓自由基催化聚合反 應製得之所謂的“低密度”聚乙烯。如此的聚合物及共聚物 係廣泛地用於製造可揉吹製薄膜。 乙稀及高碳數1-烯烴之共聚物微結構的重要特徵係為 已聚合的共單體單元沿著已聚合之乙烯單元的“主幹,,鏈分 佈。傳統的Ziegler-Natta觸媒一直以來常常產生其中已聚 合共單體單元沿著鏈叢生一起的共聚物《為了從如此的共 聚物得到特別想要的薄膜性質,每個共聚物分子裡的共單 體單元最好不叢生一起,而是沿著線性聚乙烯鏈的長度各 別佈置。近幾年來,使用以過渡金屬為底質之不連續金屬 錯合物,已提供觸媒可能的高活性且能使共單體單元的分 佈情形改善。如此的錯合物已知為金屬茂且可以以雙環戊 二稀基過渡金屬錯合物為例子。 這些以不連續金屬錯合物為底質之烯烴聚合反應觸媒 的用途現今已廣為眾所知。如此錯合物的例子可以在EP 129368,EP 206794及EP 260130裡找到。金屬茂錯合物傳 統地包括雙(環戊二烯基)锆錯合物’例如氣化雙(環戊二 烯基)錘或二氯化雙(四甲基環戊二烯基)锆。 * · — <請先閲讀背面之注意事項再填寫本頁) .裝: ,ιτ 線 24100 經濟部中央樣準局負工消费合作社印裝 Α7 Β7 五、發明説明(3 ) 在如此的觸媒系統裡,不連續金屬錯合物係在適當活 性劑存在下使用β大部分適合與如此金屬茂錯合物一起使 用的活性劑係為齒氧烷,最適合的是甲基鋁氧烷或ΜΑΟ 。其它適當的活性劑係為過氟化的硼化合物。 更近些年來,具有受抑制之幾何構造的過渡金屬錯合 物一直當做婦烴聚合反應觸媒的組份。如此的錯合物敘述 於ΕΡ 420436及ΕΡ 415815。如此的錯合物也在上述例如鋁 氧烧等活性劑的存在下使用。 然而’有利的是改良以不連續錯合物為基質之谛烴聚 合反應觸媒的功效β也有利的是使用較簡單且較不花費之 具不連續錯合物的活性劑,或使用較低的活性劑濃度。 ΕΡ 519746敘述烯烴聚合反應所用的觸媒系統,包括 具烷基黃酸酯配位基的雙(環戊二烯基)過渡金屬錯合物及 有機銘含氧化合物。如此的系統需要使用鋁氧烷當做活性 劑。 ΕΡ 591756敘述一種聚合反應觸媒系統,其包括金屬 茂錯合物與離子化合物的多陽離子錯合物。多陽離子錯合 物可以例如是二三氟甲基磺酸雙(環戊二烯基)锆 (bis(cyclopentadienyl)zirconium ditriflate)。 ΕΡ 598134敘述具螯合物形成配位基的鈦錯合物,例 如乙醮基醋酮酸酯基,其可以當做聚合烯烴與能和鈦錯合 物形成離子錯合物之化合物所用的觸媒。該參考案也明言 含螯合物形成配位基的欽隻環戊二稀化合物,例如乙醯基 醋酮酸酯基,其可以與能和金屬茂形成離子錯合物之化合 各紙張尺度逋用中國國家標準(CNS ) Α4規格(210X297命釐〉 (請先閲讀背面之注意事項再填寫本頁) -? 丁 經濟部中央橾準局—工消费合作社印製 為 2. 4 Q - A7 B7 五、發明説明(4 ) 物一起當做觸媒《所得的觸媒系統在有基鋁化合物的存在 下使用。 EP 472741敘述烯烴聚合反應觸媒,其包括具配價配 位基(例如二酿I)及紹氣烧。在此所述的錯合物不包含環戊 二烯配位基而且金屬的價數典型地滿足二氣化物配位基β 許多製備含類似二酮配位基之錯合物的方法已記載於 該項先前技術中βPrinted by the Consumers' Cooperative of the China Standards Bureau of the Ministry of Economic Affairs 4 2 4 1 η Α7 _______ Β7_ V. Description of the Invention (1) The present invention relates to a novel discontinuous metal complex, its preparation method and its application to polymerized olefins Use of catalyst composition. In particular, the present invention relates to a catalyst composition comprising a discontinuous complex and an active agent. The use of transition metals to polymerize 1-olefins, such as ethylene, is known in the prior art. The use of Ziegler-Nattta catalysts made by activating titanium halides with organometallic compounds (such as triethylammonium) is essential for many commercial methods of making smoke. In the past two decades or three decades, further technologies have been developed which have such high activity that olefin polymers and copolymers containing very low residual concentrations can be directly produced commercially. The amount of catalyst remaining in the resulting polymer is so small that it is not necessary to separate and remove it for most commercial applications. Such a method can be performed by polymerizing monomers in the gas phase, or in a solution or suspension of a diluent of a hydrocarbon. The monomers can be in the gas phase ("gas phase method," for example, by fluidizing a bed including the target polyolefin powder and desired catalyst particles using a fluidized gas stream including gaseous monomers under polymerization conditions). Polymerization is carried out. In the so-called "solution method", (co) polymerization is the introduction of monomers into a catalyst solution or suspension in a hydrocarbon diluent under conditions of temperature and pressure at which the obtained polyolefin forms a hydrocarbon dilute solution. Perform "In the" mud method ", the temperature, pressure and release solution are selected so that the resulting polyolefins form a diluted hydrocarbon suspension. These methods are usually performed at relatively low pressures (e.g. 10-50 bar) and low temperatures (e.g. 5 〇-15〇.〇 operation. Commercially produce a variety of different types and grades of commercial polyethylene. Use a transition metal as the substrate for the high polymerization of ethylene to produce the so-called `` high density, grade of poly Ethylene "These polymers have a very high hardness (please read the precautions on the back before filling this page) -Packing ·-Thread J— This paper size applies to China National Standard (CNS) a4 specifications (210 X 297 mm) 4 424100, 424100, printed by the Central Laboratories of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, this paper is printed in accordance with the Chinese National Standard (CNS) A4 specification (2IO × 2? 7 mm) A7 B7 V. Description of the invention ( 2) " and can be used to make objects that require inherent rigidity β Commercially use the copolymerization of dilute and high carbon number 1-dilute hydrocarbons (such as dilute, dilute or dilute) to obtain a variety of different densities and Other copolymers with different important physical properties. Particularly important copolymers obtained by copolymerizing ethylene with high carbon number olefins using a catalyst with a transition metal as the substrate are copolymers having a density of 0 91 0 93. These Copolymers commonly referred to in the art as "linear low-density polyethylene" are, in many respects, similar to the so-called "low-density" polyethylene produced by the high-pressure free radical polymerization of ethylene. Such polymers and Copolymers are widely used in the manufacture of kneadable blown films. An important feature of the microstructure of ethylene and high carbon number 1-olefin copolymers is that the polymerized comonomer units are along the polymerized ethylene units. "Stem, chain distribution. Traditional Ziegler-Natta catalysts have always produced copolymers in which polymerized comonomer units are clustered along chains." In order to obtain particularly desirable film properties from such copolymers, each The comonomer units in the copolymer molecule are preferably not clustered together, but are arranged separately along the length of the linear polyethylene chain. In recent years, the use of discontinuous metal complexes with transition metals as substrates has been provided. The possible high activity of the catalyst can improve the distribution of comonomer units. Such complexes are known as metallocenes and can be exemplified by dicyclopentadienyl transition metal complexes. These are discontinuous metal complexes. The use of olefins as catalysts for olefin polymerization catalysts is now widely known. Examples of such complexes can be found in EP 129368, EP 206794 and EP 260130. Metallocene complexes traditionally include bis (cyclopentadienyl) zirconium complexes such as gasified bis (cyclopentadienyl) hammer or bis (tetramethylcyclopentadienyl) zirconium dichloride. * · — ≪ Please read the notes on the back before filling this page). Packing:, ιτ 线 24100 Printed by the Central Procurement Bureau of the Ministry of Economic Affairs, Consumer Cooperatives A7 Β7 V. Description of the invention (3) In such a catalyst In the system, the discontinuous metal complex is used in the presence of a suitable active agent. Most of the active agents suitable for use with such metallocene complexes are oxyxane, the most suitable is methylalumoxane or ΜΑΟ . Other suitable active agents are perfluorinated boron compounds. In more recent years, transition metal complexes with suppressed geometric structures have been used as a component of the hydrocarbon polymerization catalyst. Such complexes are described in EP 420436 and EP 415815. Such a complex is also used in the presence of an active agent such as alumina. However, 'the advantage is to improve the effectiveness of the catalyst for the polymerization of fluorene with a discontinuous complex as the matrix. It is also advantageous to use a simpler and less expensive active agent with a discontinuous complex, or to use a lower Active agent concentration. EP 519746 describes the catalyst system used in the polymerization of olefins, including bis (cyclopentadienyl) transition metal complexes with alkyl flavate ligands and organic oxygen compounds. Such a system requires the use of alumoxane as the active agent. EP 591756 describes a polymerization catalyst system comprising a polycationic complex of a metallocene complex and an ionic compound. The polycation complex may be, for example, bis (cyclopentadienyl) zirconium ditriflate. EP 598134 describes titanium complexes with chelate-forming ligands, such as acetoacetone esters, which can be used as catalysts for polymerizing olefins and compounds capable of forming ionic complexes with titanium complexes. . This reference also explicitly states that acetocyclopentadienyl compounds containing chelate-forming ligands, such as acetoacetone ester groups, can be combined with metallocenes to form ionic complexes at various paper sizes. Use Chinese National Standard (CNS) Α4 specification (210X297 fat) (Please read the precautions on the back before filling out this page)-? Ding Central Bureau of Standards of the Ministry of Economic Affairs-Industrial Consumer Cooperatives printed 2. 4 Q-A7 B7 5. Description of the invention (4) together as a catalyst "The obtained catalyst system is used in the presence of a base aluminum compound. EP 472741 describes an olefin polymerization catalyst, which includes a coordinating ligand (such as second brewing I ) And gas-fired. The complexes described herein do not contain cyclopentadiene ligands and the valence of the metal typically satisfies the digaside ligand β. Many complexes containing similar diketone ligands are prepared. Method has been described in the prior art β
Angew. Chem Int. Ed· Engl. (1996),35(1), 80-2敘述使 用預先形成之錯隻環戊二烯-甜菜鹼陽離子製備乙醯基醋 酮酸酯基锆隻環戊二烯硼酸酯的方法。 有機金屬(1994),13(10),3897-902敘述製備(乙醯基醋 酮酸酯基)η-1-(°Λ唑-N)鍅隻環戊二烯四苯基硼酸酯。Angew. Chem Int. Ed. Engl. (1996), 35 (1), 80-2 describes the use of preformed cyclopentadiene-betaine cations to prepare ethylacetonyl zirconium cyclopentadiene. Method of enoborate. Organometallics (1994), 13 (10), 3897-902 describe the preparation of (ethanylacetone) η-1- (° Λazole-N) cyclopentadiene tetraphenylborate.
Bull. Soc. Chim. Fr. (1984), (3-4, Pt 1), 113-14 ; Z. Naturforsch., B: Anorg. Chem. Org. Chem. (1984), 39B(5), 604-6 ; Synth. React. Inorg. Met.-Org. Chem. (1983), 13(8), 1059-65; Synth. React. Inorg. Met.-Org. Chem. (1983), 13(3), 357-66和Monatsh. Chem. (1983),114(4),399-405敘述製備 金屬茂6烯基醋酮酸酯基黃酸酯及胺基甲酸酯的方法。Bull. Soc. Chim. Fr. (1984), (3-4, Pt 1), 113-14; Z. Naturforsch., B: Anorg. Chem. Org. Chem. (1984), 39B (5), 604 -6; Synth. React. Inorg. Met.-Org. Chem. (1983), 13 (8), 1059-65; Synth. React. Inorg. Met.-Org. Chem. (1983), 13 (3) , 357-66 and Monatsh. Chem. (1983), 114 (4), 399-405 describe methods for preparing metallocene 6 alkenylacetonate flavates and carbamates.
Izv. Akad. Nauk. SSSr, Ser. Khim. (1978), (11), 2645-7 敘述製備Cp2Zr(PhCOCHCOPh)(Cl)的方法。 傾發現以包括某些含雜原子之質合配位基的不連續金 屬錯合物為底質適用於聚合烯烴的觸媒系統。此外,這些 觸媒系統的特別優點為其可以在缺乏傳統鋁氧烷活性劑下 使用。 本紙張尺度適用中國國家梯準(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) .装. 訂 424100 ΓΤ Α7 Β7 經汫部中央榀羋杓只工消费合作社卬製 五、發明説明(5 因此’本發明提供一種適用於聚合婦煙的觸媒組成物 ,該組成物包括: (A)中性不連續的金屬錯合物’其通式為: (l)p MYnXmZq 其中L表不在烯烴聚合條件下保持與…鍵結的配位基 Μ是ΠΙΑ族元素或ΙΠΒ、IVB、VB、VIB或VIII過渡金 屬(CAS版本的週期表,cotton & Wilkinson第五版), Y是包括至少一個選自〇、S、N和P之中並直接與Μ 鍵結的的原子之螯合配位基, X是相同於Υ或選自下列群中:氫化物、羥基、經取 代的羥基、齒化物、過氣酸鹽、經取代的磺酸鹽、磺酸三 氟甲基酯、磺酸甲基酯、氟磺酸酯、磺酸芳酯、雙(三氟 甲基磺基)甲基、雙(三氟甲基磺基)苄基、雙(三氟甲基磺 基)醯胺、烷氧化物,芳氧化物、四烷基硼酸酯、四芳基 績酸酯、四苯基硼酸酯、經取代的四苯基硼酸酯、四(五 氟苯基)硼酸酯,四[雙(3, 5_二三氟甲基)苯基]硼酸酯,四 氟硼酸酯、六氟磷酸酯或五氟碲酸酯的基, Ζ疋中性路易斯驗, η > 或=1 . Ρ > 或=1 m >或=,〇以及 q > 或=0, 本紙張尺度通闲中國國家標準(CNS〉Α4况格(2i0x297公楚:) ----------J· ‘裝------訂-----一 成 (請先閲讀背面之注意事項寫本頁) A7 B7 4 24100 五、發明説明u ) 但有條件是n、m、p和q是滿足金屬價數的整數 或零; 和 (B)—或多種路易斯酸。 用來說明但未造成限制之本發明觸媒組成物所用的適 當不連續金屬錯合物例子為在上述通式中具有下列Y基的 金屬錯合物: 醋酮酸乙醯酯 β-二酮酸酯, β-酮酯, β-酮醛, 二硫代乙醯基醋酮酸酯, HC(S02CF3)2-, 羧酸酯, 胺基甲酸酯, 硫代羧酸酯, 二硫代羧酸酯, 硫代胺基甲酸酯, 二硫代胺基甲酸酯, 黃酸S旨, 硫代黃酸酯, 次鱗酸酯, 硫代次磷酸酯, 二硫代次磷酸酯, 二烷基二硫代磷酸酯, 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) --*-------{ -裝--------訂-----f 嫌 (請先閱讀背面之注意事項再填寫本頁) 經⑷部中央桴滓而5工消费合作牡卬製 9 04 4 經濟部中央標準局貝工消費合作社印製 Λ Α7 Β7 五、發明説明(7 ) 肺酸龍(amidinate), 雙味吐酸醋(bishnidazolate), 磷酸酯, 硫二亞胺酸酯, 醯胺酸酯, 革酚酮酸酯, 草酸鹽, 草酸酯, 硝酸鹽, 亞硝酸鹽, 碳酸鹽, 方酸 S旨(squarate), 克酮酸酯, 亞磺酸酯, 硫酸酯, 亞硫酸酯, 氟磺酸酯, 羥肪酸酯, 硫代羥肪酸酯, 二硫代羥肪酸酯。 較佳的錯合物係為其中Y基包括至少一直接與金屬鍵 結之0原子的錯合物。 特別適當的錯合物係為其中Y基為β-二酮酸酯或β-酮 酯,例如乙醯基醋酮酯或經取代的乙醯基醋酮酯,像是氟 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X 297公釐) (請先閲讀背面之注意事項再填寫本頁) -装· 10 A7 B7 五、發明説明( 化的衍生物。 特別適當的錯合物係為其中Ρ是1或2而Μ是Ρ/Β族 金屬,如錘或鈦。 特別適當的錯合物係為其中X是羥基,齒化物或三 氟甲基磺酸鹽(triflate)。 適合本發明所用的不連續金屬錯合物包括含有雙環戊 二稀基配位基的金屬茂錯合物,例如EP 129368或EP 206794所揭示者。 特別地適當的金屬茂錯合物係為具有下列通式的錯合 物: (L)pMYnXmZq — IL------4:4-- (諳先聞讀背面之注意事項再填寫本頁) 訂 經於部中央榀工消费合作杉印?水 其中L表示未經取代的或經取代的環戊二締基配位基 Μ是IVB,VB,VIB或VIII族過渡金屬(CAS版的週期 表,Cootton & Wilkinson第 5版), Y是包括至少一個選自0、S、N和P直接與Μ鍵結的 螯合配位基, X是相同於Υ或選自下列群中:氫化物、羥基、經取 代的經基、齒化物、過氣酸鹽、經取代的續酸鹽、續酸三 氟甲基醋、確酸甲基醋、氟績酸醋、績敵芳醋、雙(三氟 甲基磺基)甲基、雙(三氟甲基磺基)苄基、雙(三氟甲基磺 基)酿胺、烧氧化物、芳氧化物、四烧基棚酸醋、四芳基 石黃酸醋、四苯基蝴酸醋、經取代的四苯基蝴酸酯、四(五 本紙張尺度通用中國國家標準(CNS ) A4規格(2l〇x297公釐) 11 04 2 Α7 Β7 經濟部中央標準而只工消費合作妇印t 五、發明说明(9 氟苯基)硼酸酯、四[雙(3,5-二三氟曱基)笨基]硼酸酯、四 氟硼酸酯、六氤磷酸酯或五氟碲酸酯的基, Ζ是令性路易斯鹼, η > 或=1 ρ > 或=1 m >或=〇和 q > 或=0, 但有條件是η、m、p和q是滿足金屬價數的整數或零。 雙%戊二締基配位基可以是被烧基、芳基、稀基、芳 烷基或烷芳基取帶代或兩個取代基可以結合一起以形成結 合的環’像是節基。較佳的環戊二烯基係係被甲基取代。 當P是2 ’即當二個雙環戊二烯基存在時,其可以經由 橋基’例如藉由化學式(R2Z)p的基結合一起,其中Z是石夕 ,鍺或碳,p是1-8而R是氫或選自烴基或其組合。 較佳的錯合物係為其十Μ是錯,欽或給,p是2而11是1 或2。 也適合本發明使用的錯合物係為具有受抑制之幾何構 造的錯合物,例如ΕΡ 416815或ΕΡ 420436所揭示者。 舉例來說,具有下列通式的錯合物可以適用: Ζ — p / /Izv. Akad. Nauk. SSSr, Ser. Khim. (1978), (11), 2645-7 describe a method for preparing Cp2Zr (PhCOCHCOPh) (Cl). It has been found that the use of discontinuous metal complexes including certain heteroatom-containing ligands as substrates is suitable for catalyst systems for polymerizing olefins. In addition, these catalyst systems have the particular advantage that they can be used in the absence of traditional alumoxane active agents. This paper size is applicable to China National Standard for Ladder (CNS) A4 (210X297 mm) (please read the precautions on the back before filling out this page). Packing. Order 424100 ΓΤ Α7 Β7 Ministry of Economics and Trade Central Cooperative Consumer Cooperative Preparation 5. Description of the invention (5 Therefore, the present invention provides a catalyst composition suitable for polymerizing women's cigarettes, the composition includes: (A) a neutral discontinuous metal complex, and its general formula is: (l ) p MYnXmZq where L is a ligand that does not remain bonded to ... under olefin polymerization conditions M is a group IIIA element or a transition metal of IIB, IVB, VB, VIB, or VIII (CAS version of the periodic table, cotton & Wilkinson fifth Version), Y is a chelating ligand including at least one atom selected from 0, S, N, and P and directly bonded to M, and X is the same as Υ or selected from the group consisting of hydride, Hydroxyl, substituted hydroxyl, dentate, peroxyacid, substituted sulfonate, trifluoromethyl sulfonate, methyl sulfonate, fluorosulfonate, aryl sulfonate, bis (trifluoro Methylsulfo) methyl, bis (trifluoromethylsulfo) benzyl, bis (trifluoromethylsulfo) ) Amines, alkoxides, aryl oxides, tetraalkylborates, tetraarylates, tetraphenylborates, substituted tetraphenylborates, tetrakis (pentafluorophenyl) Borates, Tetra [bis (3, 5-ditrifluoromethyl) phenyl] borates, Tetrafluoroborate, Hexafluorophosphate or Pentafluorotellurate groups , Η > or = 1. Ρ > or = 1 m > or =, 〇 and q > or = 0, this paper standard is free of Chinese national standards (CNS> Α4 condition grid (2i0x297):-)- --------- J · 'install ------ order ----- 10% (please read the notes on the back to write this page) A7 B7 4 24100 V. Description of the invention u) But With the proviso that n, m, p, and q are integers or zeros that satisfy the valence of the metal; and (B) —or several Lewis acids. Suitable discontinuous metals used in the catalyst composition of the present invention to illustrate, but not to limit. Examples of complexes are metal complexes having the following Y groups in the above general formula: acetoacetate β-diketonate, β-ketoester, β-ketoaldehyde, dithioacetamidate Ketoester, HC (S02CF3) 2-, Carboxylate, Carbamate, Thio Acid ester, dithiocarboxylic acid ester, thiocarbamate, dithiocarbamate, flavonic acid, thioflavanate, hypophosphonate, thiophosphite, di Thiophosphite, dialkyl dithiophosphate, this paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm)-* ------- {-装 ----- --- Order ----- f Suspect (please read the notes on the back before filling out this page) Ministry of Economic Affairs Central Laboratories and 5 Industrial Consumers Cooperation System 9 04 4 Central Standards Bureau of Ministry of Economic Affairs Printed Λ Α7 Β7 V. Description of the invention (7) Lung acid (amidinate), bishnidazolate, phosphate ester, thiodiimidate, pyridoxate, geranone, grass Acid salt, oxalate, nitrate, nitrite, carbonate, squarate, ketoester, sulfinate, sulfate, sulfite, fluorosulfonate, hydroxy fatty acid Ester, thiohydroxy fatty acid ester, dithiohydroxy fatty acid ester. A preferred complex is a complex in which the Y group includes at least one 0 atom directly bonded to a metal. Particularly suitable complexes are those in which the Y group is a β-diketoester or β-ketoester, such as acetoacetone or substituted acetoacetone, such as fluorine. This paper is suitable for China. National Standard (CNS) A4 specification (210X 297 mm) (Please read the notes on the back before filling out this page)-Pack · 10 A7 B7 V. Description of the invention (Chemical derivatives. A particularly suitable complex is Where P is 1 or 2 and M is a group P / B metal, such as hammer or titanium. Particularly suitable complexes are those in which X is a hydroxyl group, a dentate or a triflate. Suitable for the present invention The discontinuous metal complexes used include metallocene complexes containing a dicyclopentadienyl ligand, such as disclosed in EP 129368 or EP 206794. Particularly suitable metallocene complexes are those having the following general formula Complex: (L) pMYnXmZq — IL ------ 4: 4-- (I read the notes on the back first and then fill out this page) L means unsubstituted or substituted cyclopentadienyl ligand M is a group IVB, VB, VIB or VIII transition metal (CAS version Periodic Table, Cotton & Wilkinson 5th Edition), Y is at least one chelating ligand selected from 0, S, N, and P directly bonded to M, and X is the same as Υ or selected from the group: Hydride, hydroxy, substituted acyl group, dentate, peroxyacid salt, substituted continuous acid salt, continuous acid trifluoromethyl vinegar, acetic acid methyl vinegar, fluoroacetic acid vinegar, dichloride, Bis (trifluoromethylsulfo) methyl, bis (trifluoromethylsulfo) benzyl, bis (trifluoromethylsulfo) fermented amine, burnt oxide, aryl oxide, tetrakistriol vinegar , Tetraaryl lutein acid vinegar, tetraphenyl butterfly acid vinegar, substituted tetraphenyl butterfly acid ester, four (five paper sizes common Chinese National Standard (CNS) A4 specifications (2 10x297 mm) 11 04 2 Α7 Β7 Central Standards of the Ministry of Economic Affairs and Consumers' Cooperative Work only. V. Description of the invention (9 fluorophenyl) borate, tetra [bis (3,5-ditrifluorofluorenyl) benzyl] borate, four Fluoroborate, hexafluorene phosphate or pentafluorotellurate, Z is a commanding Lewis base, η > or = 1 ρ > or = 1 m > or = 〇 and q > or = 0 , But conditionally η, m, p And q are integers or zeros satisfying the valence of the metal. The di% pentadienyl ligand may be an alkyl group, an aryl group, a dilute group, an aralkyl group or an alkaryl group, or two substituents may be combined. Together to form a bonded ring 'like a benzyl group. The preferred cyclopentadienyl system is substituted by a methyl group. When P is 2', that is, when two dicyclopentadienyl groups are present, they can pass through a bridging group ' For example, they are combined by the group of the chemical formula (R2Z) p, where Z is Shi Xi, germanium or carbon, p is 1-8 and R is hydrogen or selected from a hydrocarbon group or a combination thereof. The preferred complexes are those where 10M is wrong, or given, p is 2 and 11 is 1 or 2. Also suitable for use in the present invention are complexes having a suppressed geometric structure, such as those disclosed by EP 416815 or EP 420436. For example, a complex having the following general formula can be applied: Z — p / /
Cp*-- μ /\ cn, (xl 其中Cp *-μ / \ cn, (xl where
Cp*是單一η5-環戊二烯基或η5-經取代的環戊二烯基 本紙張尺度遄用中國國家榇準(CNS ) A4規格(2!0X297公釐) ·.~~Ί------f 4 丨- ί請先閱讀背面之注意事項再壤巧本頁j -訂- 12 Α7 Β7 經濟部中央揉準局貞工消費合作社印製 五、發明说明(10 ) Cp*是單一η5-環戊二烯基或η5-經取代的環戊二烯基 ,其視需要地經由Ζ-Ρ與Μ共價鍵結而且符合下列化學式 * R R R 其中每個R是氫或選自鹵素,烷基,芳香基,鹵烷基 ,烷氧基’芳氧基,甲矽烷基及其高達20個非氩原子的組 合,或二個或二個以上R基一起形成一結合的環系統。 Μ是以η5鍵結模態與環戊二烯基或經取代環戊二烯基 鍵結的結*欽或給而且價數為+3或+4。 Ζ是包括氧,硼等二價分子部分金屬或一群週期表IVA 族的元素(CAS版的週期表,Cotton & Wilkinson第5版)〇 P是與金属共價鍵結的連接基,包括氣,破,氧或硫 ,或視需要地Z和P—起形成_結合的環系統,和 X,Y,XI和m如上所定義,滿足Μ的價數。 較佳的錯合物係為其中金屬Μ為鈦,Ρ為氮而Ζ為矽的 錯合物。 可以提供本發明L配位基的其他適當錯合物係為ΕΡ 672676和ΕΡ 757996描述的錯合物。如此的錯合物包括環 辛四烯基(或COT)配位基,因此當L是環辛四烯基的時候 表示上述的化學式。 適合本發明使用的適當路易斯酸例子是例如三甲基鋁Cp * is a single η5-cyclopentadienyl or η5-substituted cyclopentadiene basic paper size, using China National Standard (CNS) A4 specification (2! 0X297 mm) ·. ~~ Ί --- --- f 4 丨-ί Please read the precautions on the back first, and then take this page j-order- 12 Α7 Β7 Printed by Zhengong Consumer Cooperative, Central Bureau of the Ministry of Economic Affairs 5. Description of invention (10) Cp * is single η5-cyclopentadienyl or η5-substituted cyclopentadienyl, which is optionally covalently bonded to M via Z-P and conforms to the following formula * RRR where each R is hydrogen or is selected from halogen, Alkyl, aryl, haloalkyl, alkoxy'aryloxy, silyl, and combinations of up to 20 non-argon atoms, or two or more R groups together form a combined ring system. M is a bond of η5 bonding mode to a cyclopentadienyl group or a substituted cyclopentadienyl group, and the valence is +3 or +4. Z is a partial metal including oxygen, boron and other metals or a group of elements of the group IVA of the periodic table (CAS version of the periodic table, Cotton & Wilkinson 5th Edition) 〇 P is a covalent bonding group with a metal, including gas , Broken, oxygen or sulfur, or Z and P together as needed to form a ring system, and X, Y, XI and m as defined above, to satisfy the valence of M. Preferred complexes are those where the metal M is titanium, P is nitrogen and Z is silicon. Other suitable complexes that can provide the L ligands of the present invention are the complexes described by EP 672676 and EP 757996. Such a complex includes a cyclooctatetraenyl (or COT) ligand, and thus when L is a cyclooctatetraenyl group, it represents the above chemical formula. An example of a suitable Lewis acid suitable for use in the present invention is, for example, trimethylaluminum
(請先閲讀背面之注意事項再填寫本頁) 訂 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) 13 424100/^ 五、發明説明(11 > 經濟部中央橾準局貞工消費合作社印製 A7 B7 等娜:合:’三異丁基紹’例如參(五氣苯細等芳 基銘化合物,例如三氩化料料化物,例如氫化二異丁 基銘,單^氟笨基)二異丁基科經混合的氳化物,芳基/ 烧基切合的是例如氣化二f基料燒基銘南 化物’或例如二氣化f基料二氣化W料烧基紹二齒 化物。 也適合當做路易斯酸使用的是烧基或芳基蝴,齒㈣ 及氫化物,例如卿十二_巨環職合物,烧基鎮或邊 化鎮也適合1別適合較參(五氟苯基)帅三異丁基蝴 Ο “例如(2’7-二甲基],8_二伸苯二氧基)雙(二異·丁基銘) 等芳氧基IS化合物’和例如兒細甲佩等芳氧基领化合 物也是適合的。 -或多種路易斯酸對本發明不連續金屬錯合物的比例 是0.2 : 10,_ ’ 較佳為 0.2 : 5000。 本發明的觸媒組成物可以適當地負載。舉例來說不 連續金屬錯合物可赠錄是氧切,氧化减氣化鎖等 觸媒載體上》可以藉由傳統技術來製備經負載的觸媒。 本發明的觸媒組成物也可以包括其它觸媒組份 ,例如(Please read the precautions on the back before filling this page) The size of the paper used for this edition applies to the Chinese National Standard (CNS) A4 specification (210X297 mm) 13 424100 / ^ V. Description of the invention (11 > Printed by the Industrial and Commercial Cooperatives, such as A7, B7, etc .: He: 'Triisobutyl Shao', for example, aryl compounds such as ginseng (pentabenzene, etc.), such as tri-argonated compounds, such as hydrogenated diisobutyl, monofluorobenzyl The diisobutyl group is mixed with a halogenated compound, and the aryl / alkyl group is combined with, for example, a gasified di-base compound, or a base, such as a gasified di-base compound, or a bi-gasified base. Bidentate. Also suitable for use as Lewis acid are alkynyl or aryl butterfly, dentate and hydride, such as Qingzhuang_macrocyclic compound, alkynyl or edge town is also suitable. (Pentafluorophenyl) Triisobutyl Butyl O "such as (2'7-dimethyl], 8-diphenylene dioxy) bis (diiso · butylming) and other aryloxy IS compounds" and for example Also suitable are aryloxy-collar compounds such as carbamide, etc.-The ratio of the Lewis acid to the discontinuous metal complex of the present invention is 0.2: 10, _ 'is preferably 0.2: 5000. The catalyst composition of the present invention can be appropriately loaded. For example, discontinuous metal complexes can be recorded on catalyst carriers such as oxygen cutting and oxidizing degassing locks. The supported catalyst can be prepared by conventional techniques. The catalyst composition of the present invention may also include other catalyst components, such as
Ziegler觸媒或其它金屬錯合物β舉例來說,可以使用包括 本發明經負載金屬錯合物及活性劑還有ziegler觸媒(例如 一種包括鈦,鎂及齒素)的複位觸媒組成物。如此的複位 觸媒可以藉由傳統路徑製備。 本發明的錯合物必要時也可以在傳統活性劑(例如鋁 本紙張尺度逋用中國國家標準(CNS ) A4規格(210x2S>7公麓) (請先聞讀背面之注意事項再填寫本頁)Ziegler catalyst or other metal complex β. For example, a reset catalyst composition including the supported metal complex and active agent of the present invention and ziegler catalyst (such as a titanium, magnesium and dentine) composition can be used. Thing. Such a reset catalyst can be prepared by a conventional route. The complex of the present invention can also be used in traditional active agents if necessary (for example, aluminum paper size using Chinese National Standard (CNS) A4 specifications (210x2S > 7 feet)) (Please read the precautions on the back before filling out this page )
14 - π 輕濟部中央標準局貝工消費合作杜印製 A7 B7 五、發明説明(12) — 氣貌尤其疋甲基銘氧烧)的存在下使用。 本發明的錯合物也可以在離子化離子化合物的存在下 使用離子化離子化合物例如是三苯甲基四(五氟苯基)硼 酸鹽一甲基鋁四(五氣苯基)硼酸鹽,鋰四(五氟苯基)硼 酸鹽—笨甲基四苯基蝴酸®,四氟IL酸和相似物。 本發明也提供一種製造聚烯烴,尤其乙烯之高聚物及 乙稀與較少量至少-種⑶⑽,較佳為C3 C8 α稀烴之共 聚物的方法。該方法包括在足以使聚合反應開始的溫度和 壓力下使單體或多種單體視需要在氫的存在下與本發明觸 媒組成物接觸β 合適的α-烯烴可以是丙烯,丙烯-1,己烯-1,4-曱基 戊烯-1和辛烯q。 本發明的烯烴聚合反應觸媒組成物可以用來使用溶液 聚合法’泥漿聚合法或氣相聚合法製造聚合物。進行如此 聚合反應的方法和裝置為眾所皆知並且敘述於例如John14-π Produced by Shellfish Consumer Cooperation of the Central Bureau of Standards of the Ministry of Light Industry A7 B7 V. Description of the invention (12)-Appearance, especially methyl sintered oxygen). The complex of the present invention can also be used in the presence of an ionized ionic compound such as trityl tetrakis (pentafluorophenyl) borate monomethylaluminum tetrakis (pentaphenyl) borate, Lithium tetrakis (pentafluorophenyl) borate—benzyltetraphenylphosphonic acid®, tetrafluoroIL acid and the like. The present invention also provides a method for producing a polyolefin, especially a polymer of ethylene and a copolymer of ethylene and a smaller amount of at least one species of cyanine, preferably a C3 C8 alpha dilute hydrocarbon. The method includes contacting a monomer or monomers with the catalyst composition of the present invention in the presence of hydrogen if necessary at a temperature and pressure sufficient to initiate the polymerization reaction. A suitable alpha-olefin may be propylene, propylene-1, Hexene-1,4-fluorenylpentene-1 and octene q. The olefin polymerization catalyst composition of the present invention can be used to produce a polymer using a solution polymerization method's slurry polymerization method or a gas phase polymerization method. Methods and apparatus for conducting such polymerizations are well known and described in, for example, John
Willey & Sons出版的聚合物科學及工程百科丨987年第7冊 第580-488頁及1988年第12冊第504-541頁。本發明觸媒可 以以相似已知烯烴聚合觸媒的數量及條件下使用。 聚合反應可以視需要地在氩的存下進行。氫和其它適 合的鏈轉移劑可以用來控制製得之聚烯烴的分子量。 本發明的另一發明内容係提供具下列通式的新穎性金 屬錯合物:Encyclopedia of Polymer Science and Engineering, published by Willey & Sons, vol. 7, pp. 580-488, and 1988, p. 504-541. The catalyst of the present invention can be used under similar amounts and conditions of known olefin polymerization catalysts. The polymerization reaction can be carried out optionally in the presence of argon. Hydrogen and other suitable chain transfer agents can be used to control the molecular weight of the polyolefin produced. Another aspect of the present invention is to provide a novel metal complex having the following general formula:
(L)2 μ Y X 本紙張尺度適用中國國家榇準(CNS ) Α4現格(2〗ΟΧ 297公釐) ^^1 - 1^1 m - - I - - i I. —^1 {請先閲讀背面之注f項再填寫本頁) -15 - A7 B7 經濟部中央橾準局負工消費合作杜印製 五、發明説明(13)(L) 2 μ YX The size of this paper is applicable to China National Standards (CNS) A4 (2〗 〖〇Χ 297mm) ^^ 1-1 ^ 1 m--I--i I. — ^ 1 {Please first Read the note f on the back and fill in this page) -15-A7 B7 Printed by the Central Bureau of Quasi-Ministry of the Ministry of Economic Affairs, Consumption Cooperation Du V. Invention Description (13)
Z——P / /Z-P / /
L——MXY 其中L表示未經取代的或經取代的雙環戊二烯基配位 基, Z是包括氧’硼等二價分子部分金屬或一群週期表IVa 族的元素(CAS版的週期表,Cootton&Wilkinson第5版)。 P是與金屬共價鍵結的連接基,包括氮,磷,氧或硫 ’或視需要地Z和P—起形成一結合的環系統,和 Μ 是 Zr,Ti 或 Hf, X是S03CF3或烴基, Y是RCOCHCOR, 其中R可以是相同或不同地,為烴基或經取代的煙基 ’例如CH3,C2HS或CF3,c(ch3)3或och2ch3。 尤其,揭示具下列化學式的錯合物: (1,3-(CH3)2CjH3)2Zr(CH3C0CHC0CH3)S03CF3 (l>3-(CH3)2CiH3)IZr(CF3COCHCOCF3)S〇3CF3 (IKCHAC^ZKCHjCOCHCOOCHjCHOSOsCFjL——MXY where L represents an unsubstituted or substituted dicyclopentadienyl ligand, and Z is a part of a metal including a bivalent molecule such as oxygen 'boron or a group of elements of Group IVa of the periodic table (CAS version of the periodic table , Cotton & Wilkinson 5th Edition). P is a linker covalently bonded to a metal, including nitrogen, phosphorus, oxygen or sulfur 'or optionally Z and P together to form a combined ring system, and M is Zr, Ti or Hf, X is S03CF3 or Hydrocarbyl, Y is RCOCHCOR, where R can be the same or different, and is a hydrocarbyl or substituted nicotyl ', such as CH3, C2HS or CF3, c (ch3) 3 or och2ch3. In particular, a complex with the following chemical formula is disclosed: (1,3- (CH3) 2CjH3) 2Zr (CH3C0CHC0CH3) S03CF3 (l > 3- (CH3) 2CiH3) IZr (CF3COCHCOCF3) S〇3CF3 (IKCHAC ^ ZKCHjCOCHCOOCHjCHOSOSOCFj
CCHJ)2Si((CH3),C5)(NC((CHs)3)Ti(CFiCOCHCOCF3)SOJCFJ (U-(CH3)2C5H3)2Zr(CH3)3CC0CHC0CH3)3)S03CF3 (CJHJ)iZr(CH3COCHCOCH3)CH3 根據本發明另一發明内容,提供一種製備新穎性錯合 物的方法,其包括使含有至少一種與金屬接連之烴基取代 本紙張尺度適用中國國家標準(CNS > A4規格(2丨0X297公釐) (請先閱讀背面之注意事項再填寫本頁) 訂 16 經濟部中央樣準局Μζ工消费合作社印製 Λ2 ά ] Ο 〇 ·ϊ; Λ Α7 _____Β7__ 五、發明説明(14 ) 基的前驅物錯合物(例如Cp2Zr(CH3)(S03CF3)與適當的二酮 在適當溶劑(例如曱苯或戊烷)裡反應並藉由過濾或去除溶 劑來回收錯合物》 因此,提供一種製備化學式Cp2-MXY之錯合物的方 法,其係藉由使化學式Cp2M(烴基)X之錯合物與化學式 RCOCH2COR之二酮在適當溶劑裡反應,其中 M=Zr,Ti 或 Hf, Y=RCOCHCOR, X=S03CF3, R=烴基》 t 如果前騍物錯合物包含多一種以上烴基取代基而且需 要所的錯合物也包含一個烴基取代基,則最好藉由將二酮 逐滴地加入前驅物錯合物的已攪拌溶液中來進行〇 因此也提供一種用來製備化學式Cp2M(烴基)Y之錯合 物的方法,其藉由用化學式RCOCH2COR之二輞來處理化 學式Cp2M(烴基)2之錯合物溶液, 其中 M = Zr,Ti,Hf Y = RCOCHCOR,和 R =煙基。 本發明現在將以下列實施例作參考進一步地舉例説明 之。 實施例1 H ^ (1,3-(CH〇X,H, VZrrCHXOCHCOCH,)SO,CF. ———w £, 本紙張尺度適用中國國家標準(CNS > Α4規格(210X297公釐) (請先閲修背面之注意事項再填寫本頁) 訂 17 經濟部中央標準局貝工消费合作社印« A7 B7 五、發明説明(15) 將88微升(1莫耳)三氟甲基磺酸加入2〇毫升甲苯裡的 307毫克(1毫莫耳)二甲基化雙(1,3-二甲基環戊二烯基)錯。 攪拌混合物一個小時,然後將1〇2微升(1莫耳)2,4戊二酮一 次加入。將溶劑蒸發至乾,將剩餘物從乙鰱/己烷再結晶, 產生 247 毫克(l,3-(CH3)2C5H3)2Zr(CH3COCHCOCH3)S03CF3 淡黃色結晶(47%產率)。 以NMR到的特徵如下: W-NMR : (d8-甲苯,周圍溫度) δ-5.63(4Η,m,Cp-CH),5.56(2H,m,Cp-CH),4·98(1Η ,s,acac CH),1.85(12H,br s,Cp-CH3),1.67(6H,br s ,acac Me) e 13C-NMR : (d8-曱苯,周圍溫度) 5=14.7(CHrCp),26.5(£Hracac),102.3(£H-acac) , 120.7 ,129.4(CH-Cp) » 19F-NMR ·· (d8-甲苯,周圍溫度) 6=-79.4 » 實施例2 盤備(1, SJCHACmZrfCFXOCHCOCIMSOXF, 一一 —*—·— 一一 將88微升(1莫耳)三氟甲基磺酸加入20毫升甲笨裡的 307毫克(1毫莫耳)二甲基化雙(1,3·二甲基環戊二烯基)鍅 。攪拌混合物一個小時,然後將141微升(1莫耳 )1,1,1,5,5,5-六氟-2,4-戊二酮一次加入。將溶劑蒸發至乾 ,將剩餘物從乙醚/己烷1/10裡再結晶,產生442毫克(丨,3_ (CH3)2C5H3)2Zr(CF3C0CHC0CF3)S03CF3 淡黃色結晶(7〇% 本纸張尺度適用中國圃家標準(CNS ) A4规格(210 X297公釐) (請先閲讀背面之注意事項再填寫本頁) 衣· 訂 經濟部中喪揉準局貝工消背合作社印装 4241 ㈣, λ: B7 五、發明説明(16 ) 產率)。 以NMR到的特徵如下: W-NMR : (d8-甲苯,周圍溫度) 5=5.99(1H,s,hfacac),5.72(2H,s,Cp-CH),5.45(1H, s,Cp-CH),1.86(6H,s,Cp-CH3),1.65(6H,s,Cp-CH3) o i3C-NMR : (d8-甲苯,周圍溫度) 5=13.83,14.02(CH3-Cp),92.31(£H3-hfacac),116.286, 117.154,123.081(CH-Cp)。 19F-NMR : (d8-曱苯,周圍溫度) 5=-77,10,-77.39,-79.41。 管施例3 盥備(UVCHAqHAZrfCI^COCHCOOCt^CHpsO.r^ 將88微升(1莫耳)三氟甲基磺酸加入20毫升甲苯裡的307毫 克(1毫莫耳)二甲基化雙(1,3-二甲基環戊二烯基)锆。攪拌混合 物一個小時,然後將127微升(1莫耳)乙基乙醯醋酸酯一次加入 。將溶劑蒸發至乾,將剩餘物從乙醚/己烷1/10裡再結晶,產生 442毫克(l,3_(CH3)2C5H3)2Zr(CH3COCHCOOCH2CH3)S03CF3 無色結晶(76%產率)。 以NMR到的特徵如下: lH-NMR : (d8-曱苯,周圍溫度) δ=5·76(2Η,s br,Cp-CH),5.63(2H,s br,Cp-CH),5·51(2Η ,s br,Cp-CH),4.82(1H,s,acac-CH),4.46(2H,s br ,OCil2CH3),190(6H’ s br’ Cp-CH3)’ 18.5(6H,s br’ Cp-CH3) 本紙浪尺度適用中國國家梯率(CNS ) A4規格(2丨0X297公釐} (請先閲讀背面之注意事項再填寫本頁) 訂 19 經濟部中央搮準局貞工消费合作社印掣 424 1 0 0 ; " A7 B7 五、發明説明(17 ) ,1_52(3H,s,br acac-CH3),1·09(3Η,s br,OCH2CH3) o 19F-NMR : (d8-曱苯,周圍溫度) 5=-78.98 -實施例4 贺備(CHASiaCHACjNCaCHAVTidCOCHCOCDSCKCF, 一一·儀—響· «·_ 應用實施例2的方法,以(CH3)2Si((CH3)4C5) (NC((CH3)3)Ti(CH3)2為起始物質,得到(CH3)2Si((CH3)4Cs) (NC((CH3)3)Ti(CF3C0CHC0CF3)S03CF3 以NMR到的特徵如下: W-NMR : (d8-甲笨,周圍溫度) δ=6.15(1Η,s,acac-CH),2.23,1.91,1.82,1·09(12Η, 4s,Cp-CH3),0·99(9Η,s,NC(CH3)3,0.48,0.39(6Η,2s ,Si-CH3)。 l9F-NMR: (d8-甲笨,周圍溫度) 5=-76.4 > -76.7 > -79.2 〇 實施例5 製備(l,3-(CH,),CJiAZr(CHACCOCHCOCH,ysnTT? 將88微升(1莫耳)三氟甲基磺酸加入20毫升甲笨裡的 307毫克(1毫莫耳)二曱基化雙(1,3·二甲基環戊二烯基)錘 。攪拌混合物一個小時,然後將208微升(1莫耳)2,2,6,6-w 甲基-3,5-戊二酮一次加入。將溶劑蒸發至乾,將剩餘物從 乙醚/己烷1/20裡再結晶,產生531毫克(1,3_ (CH3)2C5H3)2Zr(CH3)3CCOCHCOCH3)3) 本&乐尺度逋用中國國家梯準(CNS } A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) - 20 424106 A7 B7 經濟部中央梯準局另工消費合作社印裝 五、發明説明(18) S03CF3#色結晶(87%產率)。以NMR到的特徵如下: H-NMR : (d8-甲苯,周圍溫度) δ=5.67(4Η,m,CP-CH),5.63(2H,m,Cp-CH),5.8(bs ,acac CH),2.03(12H,br s,Cp-CH3),1.0(18H,br s, acac'Bu) ° l3C-NMR : (d8-甲苯,周圍溫度) 5=14.6(CH3-Cp),27.8,28.3(tBu-acac)’ 92.2(CH-acac),116.3 ,117.0,122.9(CH-CP) e 實施例6 製備(aHAZKCHXOCHCOCtUCH, 將370微升(3.6莫耳)2,4-戊二明逐滴地攪拌加入100毫 升-78°C戍烷裡的920毫克(3.6毫莫耳)二甲基化雙(1,3-二甲 基環戊二烯基)锘。在回溫到周圍溫度前攪拌混合物一個 小時。藉由過濾單離並用冷戊烷(2X50毫升)沖洗,形成 白色沉澱物。(C5H5)2Zr(CH3COCHCOCH3)CH,產率為630 毫克(52%產率)。以NMR到的特徵如下: M-NMR: (d6-苯,周圍溫度) δ=5.79(10Η,s,CP),5.08(1H,s,acac CH),1.61(6H, s,acac CH3),0.61(3H,s,CH3)。 聚合反應 實施例7-12係在1升容量的壓熱器裡使用異丁烷當做 反應介質進行。反應器加熱到85°C並以氮氣(2升/分鐘)徹 底清淨90分鐘。然後將溫度降到5〇t並將選擇過的烷基鋁 試劑及異丁烷(5〇〇毫升)導入反應器中。在75。<:下攪拌混 本紙張尺皮逋用中國國家梯準(<^5)八4規格(210父297公羞) HI n^i ^^1» I^i - -I ^-i 1^1 n^i ^fi— (請先閲讀背面之注意事項再填寫本頁) 21 A7 B7 五、發明説明(19 ) 合物(200 rpm)至少120分鐘,然後將10巴超壓的乙稀加入 。再將金屬錯合物和其它路易斯酸(如果有用的話)加入反 應器。將乙烯加入以維持反應進行中反應器的壓力一定。 以迅速地通氣反應器並冷卻至2〇°C來終止反應。固體聚合 物產物係用類甲烷的氣化氩清洗,用乙醇水溶液沖洗並乾 燥(50°C ’真空,16小時)〇所用的錯合物和路易斯酸如下 * * 實施例7 將三異丁基鋁(3毫升1 Μ甲苯裡的溶液;Aldrich)和三 甲基銘(1毫升2 Μ己烧裡的溶液;Aldrich),接著(1,3· (CH3)2C5H3)2Zr(CH3COCHCOCH3)SO3CF3(0_95微莫耳;如 實施例1裡製備)導入反應器。反應時間為66分鐘β聚合物 產率為10.22克,觸媒活性978克聚合物/毫莫耳Zr.b.he 實施例8 將三異丁基紹(4毫升1 Μ甲苯裡的溶液;Aldrich),接 著(l,3-(CH3)2CsH3)2Zr 經濟部中央揉率扃貞工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁} (CH3COCHCOCH3)SO3CF3(1.0微莫耳;如實施例⑽ 製備)和三異丁基鋁(1〇微莫耳)的混合物導入反應器。反 應時間為60分鐘。聚合物產率為23.47克,觸媒活性2347 克聚合物/毫莫耳Zr.b.h。 會施例9 將三異丁基紹(4毫升1 Μ甲苯裡的溶液;Aldrich),接 著(l,3-(CH3)2C5H3)2Zr(CH3COCHCOCH3)SO3CF3(0.95 微莫 耳’如實施例 1 裡製備)和 B(C6F5)3 (Boulder Scientific; 1.425 本紙张尺度逋用中®國家標準(CNS ) A4規格(210X 297公婕) 22 424100 A7 B7 20 五、發明説明( 微莫耳)的混合物導入反應器》反應時間為60分鐘。聚合 物產率為15.61克,觸媒活性1643克聚合物/毫莫耳Zr.b.h ύ 實施你丨]0 將三異丁基鋁(5毫升1 Μ曱苯裡的溶液;Aldrich),接 著(1,3-(CH3)2C5H3)2Zr(CF3C0CHC0CF3)S03CF3 (0.95微莫 耳:如實施例2裡製備)和B(C6F5)3 (Boulder Scientific ; 0.95 微莫耳)導入反應器。反應時間為60分鐘。聚合物產率為 21·61克,觸媒活性2275克聚合物/毫莫耳Zr.b.h。 實施例11 將三異丁基鋁(4毫升1 Μ甲苯裡的溶液;Aldrich),接 著(1,3-(CH3)2C5H3)2Zr(CH3COCHCOCH3) S03CF3 (0.95微 莫耳;如實施例3裡製備)和B(C6F5)3 (Boulder Scientific ; 0.95微莫耳)導入反應器。反應時間為60分鐘。聚合物產 率為12.19克,觸媒活性1283克聚合物/毫莫耳Zr.b.h。 實施例12 將三異丁基鋁(4毫升1 Μ甲苯裡的溶液;Aldrich),接 著(1,3-(CH3)2CsH3)2Zr(CF3C0CHC0CF3)S03CF3 (1.0微莫耳 ;如實施例2裡製備)和ΜΑΟ(Α1 ·· Ζι*比例為6〇0 : 1)導入反 應器。反應時間為60分鐘。聚合物產率為48.8克,觸媒活 性4880克聚合物/毫莫耳Zr.b*h。CCHJ) 2Si ((CH3), C5) (NC ((CHs) 3) Ti (CFiCOCHCOCF3) SOJCFJ (U- (CH3) 2C5H3) 2Zr (CH3) 3CC0CHC0CH3) 3) S03CF3 (CJHJ) iZr (CH3COCHCOCH3) CH3 Another aspect of the present invention is to provide a method for preparing a novel complex, which comprises replacing at least one hydrocarbon group connected to a metal with a paper standard of Chinese national standard (CNS > A4 specification (2 丨 0X297 mm)) Please read the notes on the back before filling in this page) Order 16 Printed by the Central Samples Bureau of the Ministry of Economic Affairs, Mζ Industrial Consumer Cooperative Λ2 ά] Ο 〇ϊ; Λ Α7 _____ Β7__ 5. The precursors of the invention description (14) are mismatched (Such as Cp2Zr (CH3) (S03CF3) and appropriate dione in an appropriate solvent (such as toluene or pentane) and recover the complex by filtering or removing the solvent.) Therefore, a preparation formula Cp2-MXY is provided The method of the complex is by reacting the complex of the chemical formula Cp2M (hydrocarbyl) X with a diketone of the chemical formula RCOCH2COR in a suitable solvent, where M = Zr, Ti or Hf, Y = RCOCHCOR, X = S03CF3 , R = hydrocarbyl "t if the precursor complex contains more than one hydrocarbyl substitution And the complex needs to contain a hydrocarbyl substituent, it is best to add the diketone dropwise to the stirred solution of the precursor complex. Therefore, a chemical formula Cp2M (hydrocarbyl group) is also provided. ) A method of a complex of Y by treating a complex solution of the chemical formula Cp2M (hydrocarbyl) 2 with the two rims of the chemical formula RCOCH2COR, where M = Zr, Ti, Hf Y = RCOCHCOR, and R = nicotyl. The present invention will now be further exemplified with reference to the following examples. Example 1 H ^ (1,3- (CH〇X, H, VZrrCHXOCHCOCH,) SO, CF. ——— w £, this paper size applies China National Standard (CNS > Α4 Specification (210X297mm) (Please read the notes on the back of the repair before filling out this page) Order 17 Printed by the Sheller Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs «A7 B7 V. Invention Description (15) 88 microliters (1 mole) of trifluoromethanesulfonic acid was added to 307 mg (1 mmol) of dimethylated bis (1,3-dimethylcyclopentadienyl) benzene in 20 ml of toluene The mixture was stirred for one hour, and then 102 microliters (1 mole) of 2,4 pentanedione was added in one portion. The solvent was evaporated to Dry and recrystallize the residue from acetamidine / hexane to give 247 mg of (l, 3- (CH3) 2C5H3) 2Zr (CH3COCHCOCH3) S03CF3 as pale yellow crystals (47% yield). The characteristics obtained by NMR are as follows: W-NMR: (d8-toluene, ambient temperature) δ-5.63 (4Η, m, Cp-CH), 5.56 (2H, m, Cp-CH), 4.98 (1Η, s , Acac CH), 1.85 (12H, br s, Cp-CH3), 1.67 (6H, br s, acac Me) e 13C-NMR: (d8- toluene, ambient temperature) 5 = 14.7 (CHrCp), 26.5 ( £ Hracac), 102.3 (£ H-acac), 120.7, 129.4 (CH-Cp) »19F-NMR · (d8-toluene, ambient temperature) 6 = -79.4» Example 2 Disk preparation (1, SJCHACmZrfCFXOCHCOCIMSOXF, 1 One — * — · — One hundred and eight microliters (1 mole) of trifluoromethanesulfonic acid was added to 20 ml of methylbenzyl 307 mg (1 mmol) of dimethylated bis (1,3 · dimethyl formaldehyde) Cyclopentadienyl) fluorene. The mixture was stirred for one hour, and then 141 microliters (1 mole) of 1,1,1,5,5,5-hexafluoro-2,4-pentanedione was added in one portion. The solvent was evaporated to dryness, and the residue was recrystallized from 1/10 of diethyl ether / hexane to produce 442 mg (丨, 3_ (CH3) 2C5H3) 2Zr (CF3C0CHC0CF3) S03CF3 of light yellow crystals (70%). Garden Standard (CNS) A4 (210 X297 mm) (Please read the precautions on the back before filling out this page) Clothing · Printed in the Ministry of Economic Affairs of the Zhuhai Bureau of Zhuhai Bureau of Carpenter Consumer Cooperative Co., Ltd. 4241 ㈣, λ: B7 V. Description of the invention (16) Yield) The characteristics obtained by NMR are as follows: W-NMR: (d8-toluene, ambient temperature ) 5 = 5.99 (1H, s, hfacac), 5.72 (2H, s, Cp-CH), 5.45 (1H, s, Cp-CH), 1.86 (6H, s, Cp-CH3), 1.65 (6H, s , Cp-CH3) o i3C-NMR: (d8-toluene, ambient temperature) 5 = 13.83, 14.02 (CH3-Cp), 92.31 (£ H3-hfacac), 116.286, 117.154, 123.081 (CH-Cp). 19F- NMR: (d8- toluene, ambient temperature) 5 = -77,10, -77.39, -79.41. Tube Example 3 Toilet (UVCHAqHAZrfCI ^ COCHCOOCt ^ CHpsO.r ^ 88 microliters (1 mole) of trifluoro Methanesulfonic acid was added to 307 mg (1 mmol) of bis (1,3-dimethylcyclopentadienyl) zirconium in 20 ml of toluene. The mixture was stirred for one hour, and then 127 μl ( 1 mole) ethylacetamidine acetate was added in one portion. The solvent was evaporated to dryness and the residue was recrystallized from 1/10 of ether / hexane to give 442 mg of (l, 3- (CH3) 2C5H3) 2Zr (CH3COCHCOOCH2CH3) S03CF3 as colorless crystals (76% yield). The characteristics obtained by NMR are as follows: lH-NMR: (d8-benzene, ambient temperature) δ = 5.76 (2Η, s br, Cp-CH), 5.63 (2H, s br, Cp-CH), 5. · 51 (2Η, s br, Cp-CH), 4.82 (1H, s, acac-CH), 4.46 (2H, s br, OCil2CH3), 190 (6H 's br' Cp-CH3) '18.5 (6H, s br 'Cp-CH3) The paper scale is applicable to China's National Slope (CNS) A4 specification (2 丨 0X297 mm) (Please read the precautions on the back before filling this page) Order 19 Consumption by the Ministry of Economic Affairs Cooperative cooperative seal 424 1 0 0; " A7 B7 V. Description of the invention (17), 1_52 (3H, s, br acac-CH3), 1.09 (3Η, s br, OCH2CH3) o 19F-NMR: (d8 -Toluene, ambient temperature 5 = -78.98-Example 4 Congratulations (CHASiaCHACjNCaCHAVTidCOCHCOCDSCKCF, one by one-instrument-ring · «· _ Apply the method of Example 2 to (CH3) 2Si ((CH3) 4C5) (NC ((CH3) 3) Ti (CH3) 2 was used as starting material to obtain (CH3) 2Si ((CH3) 4Cs) (NC ((CH3) 3) Ti (CF3C0CHC0CF3) S03CF3. The characteristics obtained by NMR are as follows: W-NMR : (d8-methylben, ambient temperature) δ = 6.15 (1Η, s, acac-CH), 2.23,1.91,1.82,1.09 (12Η, 4s, Cp-CH3), 0.99 (9Η, s, NC (CH3) 3, 0.48, 0.39 (6Η, 2s, Si-CH3). l9F-NMR: (d8-methylbenzyl, ambient temperature) 5 = -76.4 > -76.7 > -79.2 〇Example 5 Preparation of (l, 3- (CH,), CJiAZr (CHACCOCHCOCH, ysnTT?) 88 microliters (1 mole) of trifluoromethanesulfonic acid was added to 20 ml of methylbenzyl 307 mg (1 millimolar) difluorenyl Bis (1,3 · dimethylcyclopentadienyl) hammer. Stir the mixture for one hour and then 208 microliters (1 mole) of 2,2,6,6-w methyl-3,5-pentane Dione was added in one portion. The solvent was evaporated to dryness and the residue was recrystallized from diethyl ether / hexane 1/20 to yield 531 mg (1,3_ (CH3) 2C5H3) 2Zr (CH3) 3CCOCHCOCH3) 3) Ben & Le Standards: China National Standard for Ladder (CNS) A4 (210X297 mm) (Please read the precautions on the back before filling this page)-20 424106 A7 B7 Explanation (18) S03CF3 # color crystal (87% yield). The characteristics obtained by NMR are as follows: H-NMR: (d8-toluene, ambient temperature) δ = 5.67 (4Η, m, CP-CH), 5.63 (2H, m, Cp-CH), 5.8 (bs, acac CH) , 2.03 (12H, br s, Cp-CH3), 1.0 (18H, br s, acac'Bu) ° lC-NMR: (d8-toluene, ambient temperature) 5 = 14.6 (CH3-Cp), 27.8, 28.3 ( tBu-acac) '92.2 (CH-acac), 116.3, 117.0, 122.9 (CH-CP) e Example 6 Preparation (aHAZKCHXOCHCOCtUCH, 370 microliters (3.6 moles) of 2,4-pentamin was dropped dropwise Add 920 mg (3.6 millimoles) of dimethylated bis (1,3-dimethylcyclopentadienyl) fluorene in 100 ml of -78 ° C oxane. Stir the mixture before warming to ambient temperature. Hours. Isolated by filtration and rinsed with cold pentane (2X50 ml) to form a white precipitate. (C5H5) 2Zr (CH3COCHCOCH3) CH, yield 630 mg (52% yield). The characteristics obtained by NMR are as follows: M-NMR: (d6-benzene, ambient temperature) δ = 5.79 (10Η, s, CP), 5.08 (1H, s, acac CH), 1.61 (6H, s, acac CH3), 0.61 (3H, s, CH3 ). Polymerization Examples 7-12 were performed in a 1-liter autoclave using isobutane as the reaction medium. Reactor Heat to 85 ° C and clean thoroughly with nitrogen (2 liters / minute) for 90 minutes. Then lower the temperature to 50t and introduce the selected alkylaluminum reagent and isobutane (500ml) into the reactor . At 75. <: Mix the paper ruler under the paper with the Chinese national standard (&^; 5) 8 4 size (210 father 297 male shame) HI n ^ i ^^ 1 »I ^ i--I ^ -i 1 ^ 1 n ^ i ^ fi— (Please read the notes on the back before filling out this page) 21 A7 B7 V. Description of the invention (19) Compound (200 rpm) for at least 120 minutes, and then 10 bar super Pressurized ethylene is added. Metal complexes and other Lewis acids (if useful) are added to the reactor. Ethylene is added to keep the reactor pressure constant while the reaction is in progress. To quickly vent the reactor and cool to 2 ° C. ° C to stop the reaction. The solid polymer product was washed with methane-like gasified argon, rinsed with ethanol aqueous solution and dried (50 ° C 'vacuum, 16 hours). The complexes and Lewis acids used are as follows * * Example 7 Combine triisobutylaluminum (3 ml of 1 M in toluene; Aldrich) and trimethylamine (1 ml of 2 M in hexane; Aldrich). (1,3 · (CH3) 2C5H3) 2Zr (CH3COCHCOCH3) SO3CF3 (0-95 micromolar; prepared as in Example 1) was introduced into the reactor. The reaction time was 66 minutes. The yield of the beta polymer was 10.22 g, and the catalytic activity was 978 g of polymer per millimolar Zr.b.he. Example 8 Triisobutylsauric acid (4 ml of a 1 M solution in toluene; Aldrich) , Followed by (l, 3- (CH3) 2CsH3) 2Zr Printed by the Central Ministry of Economic Affairs and the Cooperative Consumer Cooperative (Please read the precautions on the back before filling this page) (CH3COCHCOCH3) SO3CF3 (1.0 micromolar; if implemented Example ⑽ Preparation) and a mixture of triisobutylaluminum (10 micromolar) was introduced into the reactor. The reaction time was 60 minutes. The polymer yield was 23.47 g, and the catalytic activity was 2347 g polymer / mmole Zr.bh Example 9 Triisobutyl succinate (4 ml of a 1 M solution in toluene; Aldrich), followed by (l, 3- (CH3) 2C5H3) 2Zr (CH3COCHCOCH3) SO3CF3 (0.95 micromolar) as in Example 1 Prepared) and B (C6F5) 3 (Boulder Scientific; 1.425 paper standard in use® National Standard (CNS) A4 specification (210X 297 male)) 22 424100 A7 B7 20 V. Description of the invention (micromolar) "Introduction to the reactor" The reaction time is 60 minutes. The polymer yield is 15.61 g, and the catalyst activity is 1643 g polymer / mmol. Zr.bh Put it into practice 丨] 0 Triisobutylaluminum (5 ml of 1 μL in benzene; Aldrich), then (1,3- (CH3) 2C5H3) 2Zr (CF3C0CHC0CF3) S03CF3 (0.95 micromolar : As prepared in Example 2) and B (C6F5) 3 (Boulder Scientific; 0.95 micromolar) were introduced into the reactor. The reaction time was 60 minutes. The polymer yield was 21 · 61 g, and the catalyst activity was 2275 g of polymer / Millimoles Zr.bh. Example 11 Triisobutylaluminum (4 ml of a 1 M solution in toluene; Aldrich) followed by (1,3- (CH3) 2C5H3) 2Zr (CH3COCHCOCH3) S03CF3 (0.95 micromoles As prepared in Example 3) and B (C6F5) 3 (Boulder Scientific; 0.95 micromolar) were introduced into the reactor. The reaction time was 60 minutes. The polymer yield was 12.19 g, and the catalyst activity was 1283 g polymer / mmol. Ear Zr.bh. Example 12 Triisobutylaluminum (4 ml of a 1 M solution in toluene; Aldrich) followed by (1,3- (CH3) 2CsH3) 2Zr (CF3C0CHC0CF3) S03CF3 (1.0 micromolar; as (Prepared in Example 2) and MAO (A1 · · Z1 * ratio of 6000: 1) were introduced into the reactor. The reaction time was 60 minutes. The polymer yield was 48.8 g and the catalyst activity was 4880 g polymer / mmol Zr.b * h.
資施例U 將三異丁基銘(4毫升1 Μ甲苯裡的溶液;Aldrich),接 著(l,3-(CH3)2C5H3)2Zr(CH3C0CHC0CH3)S03CF3 (0.95微莫 本紙張尺度適财關_準(CNS)从祕(2iQX297公瘦) 11^ - I I - _ — ^^^1 n Ε (請先聞讀背面之注意事項再填寫本頁) 經濟部中央梯準局負工消費合作社印製 23 A7 ____£ 五、發明説明(21) 耳;如實施例3裡製備)和[CPh3】[B(C6F5)4] (Boulder Scientific ; 1.43微莫耳)導入反應器。反應時間為60分鐘 。聚合物產率為37.8克,觸媒活性3979克聚合物/毫莫耳 Zr.b.h。 實施例14 將40毫升甲苯裡的三異丁基鋁(2.5毫升1 Μ甲苯裡的 溶液;Aldrich)加入(C5H5)2Zr(CH3COCHCOCH3)Me( 17.5毫 克,〇_〇5毫莫耳;如實施例6裡製備)和B(C6F5)3 (25.6毫克 ,0.05微莫耳)。將溶液在減壓下除氣並以乙烯大氣回填 。在進行60分鐘期間,打開溶液靜置以在一大氣壓下供應 乙烯並劇烈攪拌。聚合反應係藉由加入稀釋的HC1(大約40 毫升)而終止並攪拌30分鐘以溶解烷基剩餘物》固體聚乙 烯係從反應中過濾,用酸化的甲醇沖洗並在4〇t減壓下乾 燥隔夜〇聚乙烯的產率為8.94克》 (請先閲讀背面之注意事項再填寫本頁) 訂 經濟部中央標率局貝工消貧合作社印褽 24Example U Triisobutyl Ming (4 ml of a 1 M solution in toluene; Aldrich), followed by (l, 3- (CH3) 2C5H3) 2Zr (CH3C0CHC0CH3) S03CF3 (0.95 micromole CNS) Cong Mi (2iQX297 male thin) 11 ^-II-_ — ^^^ 1 n Ε (Please read the precautions on the back before filling out this page) Printed by the Central Consumers ’Bureau of the Ministry of Economic Affairs and Consumer Cooperatives 23 A7 ____ £ 5. Description of the invention (21) ear; prepared as in Example 3) and [CPh3] [B (C6F5) 4] (Boulder Scientific; 1.43 micromoles) were introduced into the reactor. The reaction time is 60 minutes. The polymer yield was 37.8 g and the catalytic activity was 3979 g polymer / mmol Zr.b.h. Example 14 Triisobutylaluminum in 40 ml of toluene (2.5 ml of a 1 M solution in toluene; Aldrich) was added to (C5H5) 2Zr (CH3COCHCOCH3) Me (17.5 mg, 0-5 mol; as in the example 6)) and B (C6F5) 3 (25.6 mg, 0.05 micromolar). The solution was degassed under reduced pressure and backfilled with ethylene atmosphere. During the 60 minutes, the solution was opened to stand to supply ethylene at atmospheric pressure and stirred vigorously. The polymerization was terminated by adding diluted HC1 (approximately 40 ml) and stirred for 30 minutes to dissolve the alkyl residue. The solid polyethylene was filtered from the reaction, rinsed with acidified methanol and dried under reduced pressure of 40 t. Overnight 〇 The yield of polyethylene is 8.94 grams "(please read the precautions on the back before filling this page).
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GBGB9619081.4A GB9619081D0 (en) | 1996-09-12 | 1996-09-12 | Polymerization catalyst |
GBGB9714386.1A GB9714386D0 (en) | 1997-07-08 | 1997-07-08 | Polymerisation catalyst |
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TW89101189A TW510906B (en) | 1996-09-12 | 1997-09-11 | Process for the polymerisation of ethylene or copolymerisation of ethylene and alpha-olefin and method for preparing complexes |
TW86113216A TW424100B (en) | 1996-09-12 | 1997-09-11 | Polymerisation catalyst |
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EP (1) | EP0925312A1 (en) |
JP (1) | JP2001500550A (en) |
AR (1) | AR009777A1 (en) |
AU (1) | AU4128997A (en) |
EG (1) | EG21243A (en) |
ID (1) | ID22033A (en) |
NO (1) | NO991190L (en) |
TW (2) | TW510906B (en) |
WO (1) | WO1998011144A1 (en) |
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US6339134B1 (en) | 1999-05-06 | 2002-01-15 | Univation Technologies, Llc | Polymerization process for producing easier processing polymers |
US6281306B1 (en) | 1999-12-16 | 2001-08-28 | Univation Technologies, Llc | Method of polymerization |
US7056996B2 (en) | 2000-02-18 | 2006-06-06 | E. I. Du Pont De Nemours And Company | Productivity catalysts and microstructure control |
US6579823B2 (en) | 2000-02-18 | 2003-06-17 | Eastman Chemical Company | Catalysts containing per-ortho aryl substituted aryl or heteroaryl substituted nitrogen donors |
US6605677B2 (en) | 2000-02-18 | 2003-08-12 | Eastman Chemical Company | Olefin polymerization processes using supported catalysts |
US6706891B2 (en) | 2000-11-06 | 2004-03-16 | Eastman Chemical Company | Process for the preparation of ligands for olefin polymerization catalysts |
WO2005108442A1 (en) | 2002-10-15 | 2005-11-17 | Exxonmobil Chemical Patents Inc. | Polyolefin adhesive compositions and articles made therefrom |
US7223822B2 (en) | 2002-10-15 | 2007-05-29 | Exxonmobil Chemical Patents Inc. | Multiple catalyst and reactor system for olefin polymerization and polymers produced therefrom |
RU2339650C2 (en) | 2003-03-21 | 2008-11-27 | Дау Глобал Текнолоджиз, Инк. | Method for olefin polymerisation with adjustable morphology |
CA2591662C (en) | 2004-12-17 | 2014-01-28 | Dow Global Technologies Inc. | Rheology modified relatively high melt strength polyethlene compositions and methods of making pipes, films, sheets, and blow molded articles |
EP1803747A1 (en) | 2005-12-30 | 2007-07-04 | Borealis Technology Oy | Surface-modified polymerization catalysts for the preparation of low-gel polyolefin films |
PL2016127T3 (en) | 2006-05-02 | 2010-08-31 | Dow Global Technologies Inc | High-density polyethylene compositions, method of making the same, articles made therefrom, and method of making such articles |
US7456244B2 (en) | 2006-05-23 | 2008-11-25 | Dow Global Technologies | High-density polyethylene compositions and method of making the same |
CN101490163A (en) | 2007-05-02 | 2009-07-22 | 陶氏环球技术公司 | High-density polyethylene compositions, method of making the same, injection molded articles made therefrom, and method of making such articles |
US7981517B2 (en) | 2007-08-28 | 2011-07-19 | Dow Global Technologies Inc. | Bituminous compositions and methods of making and using same |
TW200932762A (en) | 2007-10-22 | 2009-08-01 | Univation Tech Llc | Polyethylene compositions having improved properties |
CN101939343B (en) | 2007-12-18 | 2013-10-02 | 尤尼威蒂恩技术有限责任公司 | Method for controlling bimodal catalyst activity during polymerization |
US8148481B2 (en) | 2008-12-18 | 2012-04-03 | Univation Technologies, Llc | Method for seed bed treatment for a polymerization reaction |
BRPI1005286A2 (en) | 2009-01-30 | 2016-07-05 | Dow Global Technologies Llc | high density polyethylene composition, method for producing a high density polyethylene composition, closure device and method for producing a closure device |
IN2015DN03815A (en) | 2012-12-28 | 2015-10-02 | Univation Tech Llc | |
CN110452318A (en) | 2013-01-14 | 2019-11-15 | 尤尼威蒂恩技术有限责任公司 | Method for preparing high yield catalyst system |
WO2016086039A1 (en) | 2014-11-25 | 2016-06-02 | Univation Technologies, Llc | Methods of controlling polyolefin melt index |
RU2736937C2 (en) | 2015-05-08 | 2020-11-23 | Эксонмобил Кемикэл Пейтентс Инк. | Polymerisation method |
WO2018063767A1 (en) | 2016-09-27 | 2018-04-05 | Exxonmobil Chemical Patents Inc. | Polymerization process |
WO2018063764A1 (en) | 2016-09-27 | 2018-04-05 | Exxonmobil Chemical Patents Inc. | Polymerization process |
WO2018063765A1 (en) | 2016-09-27 | 2018-04-05 | Exxonmobil Chemical Patents Inc. | Polymerization process |
WO2018118155A1 (en) | 2016-12-20 | 2018-06-28 | Exxonmobil Chemical Patents Inc. | Polymerization process |
WO2019118073A1 (en) | 2017-12-13 | 2019-06-20 | Exxonmobil Chemical Patents Inc. | Deactivation methods for active components from gas phase polyolefin polymerization process |
WO2019173030A1 (en) | 2018-03-08 | 2019-09-12 | Exxonmobil Chemical Patents Inc. | Methods of preparing and monitoring a seed bed for polymerization reactor startup |
WO2019217173A1 (en) | 2018-05-02 | 2019-11-14 | Exxonmobil Chemical Patents Inc. | Methods for scale-up from a pilot plant to a larger production facility |
EP3788081A1 (en) | 2018-05-02 | 2021-03-10 | ExxonMobil Chemical Patents Inc. | Methods for scale-up from a pilot plant to a larger production facility |
WO2020014138A1 (en) | 2018-07-09 | 2020-01-16 | Exxonmobil Chemical Patents Inc. | Polyethylene cast films and methods for making the same |
EP3826833A1 (en) | 2018-07-26 | 2021-06-02 | ExxonMobil Chemical Patents Inc. | Multilayer foam films and methods for making the same |
WO2020102380A1 (en) | 2018-11-13 | 2020-05-22 | Exxonmobil Chemical Patents Inc. | Polyethylene blends and films |
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WO2020163079A1 (en) | 2019-02-06 | 2020-08-13 | Exxonmobil Chemical Patents Inc. | Films and backsheets for hygiene articles |
WO2021126458A1 (en) | 2019-12-17 | 2021-06-24 | Exxonmobil Chemical Patents Inc. | Films made of polyethylene blends for improved sealing performance and mechanical properties |
US12152135B2 (en) | 2020-03-12 | 2024-11-26 | Exxonmobil Chemical Patents Inc. | Films made of polyethylene blends for improved bending stiffness and high MD tear resistance |
EP4330294A1 (en) | 2021-04-30 | 2024-03-06 | ExxonMobil Chemical Patents Inc. | Processes for transitioning between different polymerization catalysts in a polymerization reactor |
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US5409874A (en) * | 1991-06-20 | 1995-04-25 | Mitsui Petrochemical Industries, Ltd. | Catalyst for olefin polymerization, process for the polymerization of olefin, and transition metal compound employable for the catalyst |
DE69322225T2 (en) * | 1992-09-22 | 1999-05-12 | Idemitsu Kosan Co. Ltd., Tokio/Tokyo | Polymerization catalysts and processes for the production of polymers |
JP3332051B2 (en) * | 1992-12-18 | 2002-10-07 | 出光興産株式会社 | Polymerization catalyst and method for producing polymer using the catalyst system |
US5543480A (en) * | 1994-06-28 | 1996-08-06 | The Dow Chemical Company | Polymerization process using diene containing catalysts |
JPH08134122A (en) * | 1994-11-11 | 1996-05-28 | Idemitsu Kosan Co Ltd | Polymerization catalyst and method for producing styrenic polymer using the same |
US5527752A (en) * | 1995-03-29 | 1996-06-18 | Union Carbide Chemicals & Plastics Technology Corporation | Catalysts for the production of polyolefins |
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1997
- 1997-09-05 EP EP97939065A patent/EP0925312A1/en not_active Withdrawn
- 1997-09-05 WO PCT/GB1997/002419 patent/WO1998011144A1/en not_active Application Discontinuation
- 1997-09-05 JP JP10513353A patent/JP2001500550A/en not_active Withdrawn
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- 1997-09-11 TW TW86113216A patent/TW424100B/en not_active IP Right Cessation
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EP0925312A1 (en) | 1999-06-30 |
TW510906B (en) | 2002-11-21 |
NO991190D0 (en) | 1999-03-11 |
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ID22033A (en) | 1999-08-26 |
JP2001500550A (en) | 2001-01-16 |
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