TW389772B - A catalyst system to produce highly crystalline polypropylene - Google Patents

A catalyst system to produce highly crystalline polypropylene Download PDF

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TW389772B
TW389772B TW85112303A TW85112303A TW389772B TW 389772 B TW389772 B TW 389772B TW 85112303 A TW85112303 A TW 85112303A TW 85112303 A TW85112303 A TW 85112303A TW 389772 B TW389772 B TW 389772B
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catalyst
compound
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TW85112303A
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Chinese (zh)
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Edwar S Shamshoum
Sehyun Kim
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Fina Technology
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附件2 :第 85112303 號專利申請案 中文說明書修正頁 民國88年f月修正 五、發明說明(17) 經濟部智慧財產局員工消費合作社印製Appendix 2: Patent Application No. 85112303 Amendment to the Chinese Manual Revised in March of the Republic of China Fifth, the description of the invention (17) Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs

對照 TEA1 CMDS 例 mmol mmol 1 1 2 2 1 1 3 1 0.5 4 1 0.1 5 1 0.05 6 1 0.033 7 1 0.02 8 1 0.01 g 1 0.002 PIPS 10 1 2 11 1 1 12 1 0.5 13 1 0.1 14 1 0.05 15 1 0.033 ptps 16 1 «0 2 17 1 1 18 1 0. 5 CPDS A1 /Si 表2 觸媒 m or 產量 β _ 0.5 10 48 1. 0 10 142 2. 0 10 205 10 10 269 20 10 249 30 10 269 50 10 280 100 10 302 500 10 294 0.5 10 163 1.0 10 214 2.0 10 294 10 10 305 20 10 249 30 10 243 0.5 10 274 1.0 10 246 2.0 10 309 B8QS〇msL·,Λ 日— 補炙 二甲苯可 等規性 溶物.wt% % in m τη m 4.1 0.9 1.5 1.4 95 2.8 7.1 8.7 6.8 93.6 15. 7 91. 6 2.9 92.2 3.1 95 2.9 96 2.4 2.5 2-8 3.9 3.1 96 3.7 (請先閱讀背面之注意事項再填寫本頁) -^fv '裝--------訂----- 本紙張尺度適用中國國家標準(CNS)A4規格(210x297公芨) -20 - 經濟部中央橾準局負工消费合作杜印袈 A7 ___B7_ 五、發明説明(1 ) 技藝: 本發明提供一種觸媒系統,其供丙烯聚合物,以產生 高晶性聚丙烯,該系統包含習用經擔髏化吉格列-那塔觭 媒與具有通式S i R„(OR / ) 之電子予體化合物之 組成物,其中R選自包括烷基,環烷基,芳基及乙烯基; R —爲烷基:而m爲0 — 3,其中當R爲烷基時,R可與 相同;當m爲〇,1或2時,則R/基可相同或相異 •‘當m爲1,2或3時,R基可相同或相異•電子予髏以 具有下式者爲隹: 0¾Control TEA1 CMDS Example mmol mmol 1 1 2 2 1 1 3 1 0.5 4 1 0.1 5 1 0.05 6 1 0.033 7 1 0.02 8 1 0.01 g 1 0.002 PIPS 10 1 2 11 1 1 12 1 0.5 13 1 0.1 14 1 0.05 15 1 0.033 ptps 16 1 «0 2 17 1 1 18 1 0. 5 CPDS A1 / Si Table 2 Catalyst m or output β _ 0.5 10 48 1. 0 10 142 2. 0 10 205 10 10 269 20 10 249 30 10 269 50 10 280 100 10 302 500 10 294 0.5 10 163 1.0 10 214 2.0 10 294 10 10 305 20 10 249 30 10 243 0.5 10 274 1.0 10 246 2.0 10 309 B8QS〇msL ·, Λ day — supplemental xylene Isotactic solution.wt%% in m τη m 4.1 0.9 1.5 1.4 95 2.8 7.1 8.7 6.8 93.6 15. 7 91. 6 2.9 92.2 3.1 95 2.9 96 2.4 2.5 2-8 3.9 3.1 96 3.7 (Please read the Please fill in this page again for attention)-^ fv 'Packing -------- Order ----- This paper size is applicable to China National Standard (CNS) A4 (210x297 cm) -20-Central Ministry of Economic Affairs Quasi-office consumer cooperation Du Yin 袈 A7 ___B7_ V. Description of the invention (1) Skills: The present invention provides a catalyst system for supplying propylene polymers to produce A crystalline polypropylene, the system comprising a composition of a conventionally-transformed Giglia-Natta medium and an electron donor compound having the general formula S i R „(OR /), wherein R is selected from the group consisting of an alkyl group, Cycloalkyl, aryl, and vinyl; R — is alkyl: and m is 0 — 3, where R can be the same when R is alkyl; when m is 0, 1 or 2, R / Can be the same or different • 'When m is 1, 2 or 3, the R groups can be the same or different • The electrons have the following formula as 隹: 0¾

Si— R4 〇r3 其中尺1爲烷基或環烷基,含有鍵結於矽原子之一級,二 級或三級碳原子;R2&R3爲烷基或芳基,而R4爲烷基 或環烷基,其二級或三級碳原子係鍵結於矽原子,RiS r4可相同或相異*而112及113可相同或相異。 先前技藝描述: 用於嫌烴聚合之觸媒系統爲技藝界所熟知者。此等觸 媒一般包含吉格列-那塔型聚合觸媒;輔觸媒,通常爲有 機鋁化合物:及電子予體,通常爲有機砂化合物·該觸媒 系統之實例示於USP4,107,413 ; 4, 294,721:4,439, 540; 本紙張尺度適用中國國家標準(CNS ) A4说格(210 X297公釐) I el. 「--_ 1^— ....... 1 .......- —1— ----- 、(請&讀背面之注意事項再填寫本頁) -4 - 經濟部中央橾準局貝工消费合作社印輦 A7 B7 五、發明説明(2 ) 4,115,319:4,220,554; 4,460,701;及4,562,173中;此等專 利之掲示在此供作參考。此等專利僅爲所申請專利中之某 部分事實’有關主要用於聚合丙烯及乙烯之觭媒及觸媒系 統· 習用經單體化吉格列-那塔聚合觸媒通常包含由例如 鈦’鉻或釩之過渡金屬之鹵化物,與金屬氫化物及/或金 屬烷基化物(一般爲有機鋁化合物)所形成之錯合物。該 觸媒通常包含於鎂化合物上擔體化而與烷基鋁鎗合之鈦鹵 化物。可添加外來電子予體或選擇性控制劑(SCA), 以改善觸媒之立體規則性,而產生更多晶狀聚合物· 此等聚合觸媒之發展具有改良之觸媒及聚合物性質。 除了改良型觸媒之外,改良之活化方法亦增加觸媒效率。 一種改良之活化方法包括在將觸媒導入反應區之前,即時 地使觸媒預先聚合之過程*該類預聚過程中之一種掲示於 USP 4,767,73 5中,其揭示在此供作參考。 除了新穎觸媒及新穎反應方法之發展之外,亦發現一 種與經擔髖化之吉格列-那塔觸媒一起作用,以形成整體 觸媒系統之適當電子予體,於聚合界具有極大之優勢,使 觸媒及聚合物性質產生巨幅改善•於此種觸媒系統中,相 信辅觸媒使觸媒活化,而使聚合物鍵起始•與經擔體化吉 格列-那塔觸媒成份一起作用而具有良好效果之輔觸媒爲 有機鋁化合物,通常爲烷基鋁,而三烷基鋁最典型,諸如 三乙基鋁(ΤΕΑβ)或三異丁基鋁(TIBAj^) ·可 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) -------CI— (請$讀背面之注ί項再填寫本頁) 訂 -5 - 經濟部中央標準局貝工消费合作杜印製 A7 B7 五、發明説明(3 ) 於習用經擔體化吉格列-那塔觸媒成份中充作觸媒之其他 有機鋁化合物包括烷基鋁二鹵化物及二烷基鋁鹵化物· 電子予體化合物係於聚合反應中減少聚合物之不規則 形式,以控制並增加立證規則性或晶狀聚合物之生產•雖 然有許多化合物皆爲眾所周知之電子予體,但特別之觸媒 可能具有與彼特別相容之特定化合物或化合物群•極期望 可發現適當類型之觸媒,產生良好之觸媒效率,並改良所 需聚合物產物之等規性之控制性及產物之其他性質*有一 種電子予髏揭示於USP4,927,797中* 本發明包括另外一項發現•意外地發現特定矽烷化合 物作爲電子予體而與特定觸媒結合時,使所製聚合物之結 晶性較由該特定觸媒和其他觸媒系統所得之先前已知結晶 性大幅增加。 發明簡述 本發明提供一種用於丙烯聚合之觸媒系統,其中該系 統包括特定觸媒與特定電子予體化合物之組合物,其使聚 合物產物之結晶性巨幅增高。該觸媒包含習用經擔體化吉 格列-那塔觸媒成份,有機鋁辅觸媒及有機矽電子予體· 該組合物產生一種觸媒系統,其產生結晶性大幅高於(二 甲苯可溶物較少)如以下對照例所說明之先前觸媒所提供 者之聚合物產物•此外,使用特定習用經檐體化吉格列-那塔觸媒成份之本發明觸媒系統,與其他類型之觸媒成份 比較之下,對聚合物產物之二甲苯可溶物提供較佳之控制 本紙張尺度適用中國國家揉準(CNS > A4規格(210X297公釐) ! ^ 丨 — CI — (請$讀背面之注意事項再填寫本頁)Si— R4 〇r3 Wherein 1 is an alkyl or cycloalkyl group, which contains a first-, second- or third-order carbon atom bonded to a silicon atom; R2 & R3 is an alkyl or aryl group, and R4 is an alkyl or ring Alkyl, whose secondary or tertiary carbon atoms are bonded to a silicon atom, RiS r4 may be the same or different * and 112 and 113 may be the same or different. Prior art description: Catalyst systems for the polymerization of hydrocarbons are well known in the art world. These catalysts generally include Giglia-Natta type polymerization catalysts; auxiliary catalysts, usually organoaluminum compounds: and electron donors, usually organic sand compounds. Examples of this catalyst system are shown in USP 4,107, 413; 4, 294, 721: 4, 439, 540; This paper size applies the Chinese National Standard (CNS) A4 format (210 X297 mm) I el. "--_ 1 ^-....... 1 .......- —1— -----, (Please & read the notes on the back and fill in this page again) -4-Central Laboratories of the Ministry of Economy 4. Description of the invention (2) 4,115,319: 4,220,554; 4,460,701; and 4,562,173; the list of these patents is hereby incorporated by reference. These patents are for application only. Some of the facts in the patent are related to catalysts and catalyst systems mainly used to polymerize propylene and ethylene. Conventional monomerized Giglia-Nata polymerization catalysts typically contain A halide, a complex formed with a metal hydride and / or a metal alkyl compound (generally an organoaluminum compound). The catalyst is usually supported on a magnesium compound and Aluminium alkylated titanium halides. External electron donors or selective control agents (SCA) can be added to improve the three-dimensional regularity of the catalyst and produce more crystalline polymers. Development of these polymerization catalysts It has improved catalyst and polymer properties. In addition to the improved catalyst, the improved activation method also increases the efficiency of the catalyst. An improved activation method includes pre-polymerizing the catalyst immediately before introducing the catalyst into the reaction zone. Process * One of this type of pre-polymerization process is shown in USP 4,767,73 5 and its disclosure is here for reference. In addition to the development of new catalysts and novel reaction methods, a kind of Giglia-Nata catalysts work together to form a suitable electron donor for the overall catalyst system, which has a great advantage in the polymerization industry, and greatly improves the properties of catalysts and polymers. In the system, it is believed that the auxiliary catalyst activates the catalyst and initiates the polymer bond. • The auxiliary catalyst that works well with the supported Giglia-Nata catalyst component is an organoaluminum compound, usually Aluminum alkyl Trialkylaluminium is the most typical, such as triethylaluminum (TEAβ) or triisobutylaluminum (TIBAj ^). The Chinese paper standard (CNS) A4 specification (210X297 mm) can be applied to this paper size ---- --- CI— (Please read the note on the back of the page and fill in this page again) Order-5-Printed by Alabaster Consumer Cooperatives, Central Bureau of Standards, Ministry of Economic Affairs, printed A7 B7 V. Description of the invention Other organoaluminum compounds that act as catalysts in Giglia-Nata catalyst components include alkyl aluminum dihalides and dialkyl aluminum halides. Electron donor compounds are used to reduce irregular forms of polymers during polymerization. To control and increase the production of legislative regularity or crystalline polymers. • Although many compounds are well-known electron donors, special catalysts may have specific compounds or groups of compounds that are particularly compatible with them. • High expectations Appropriate types of catalysts can be found, producing good catalyst efficiency, and improving the isotacticity of the desired polymer product and other properties of the product. * An electron is disclosed in USP 4,927,797. * This Invention includes another discovery Silane been found that a particular compound binds to a specific catalyst and an electronic member to the crystallinity of the produced polymer compared to the previously known a substantial increase in crystallinity of the resultant specific catalyst and other catalyst systems. SUMMARY OF THE INVENTION The present invention provides a catalyst system for propylene polymerization, wherein the system includes a combination of a specific catalyst and a specific electron donor compound, which greatly increases the crystallinity of the polymer product. The catalyst contains the conventionally-supported Giglia-Nata catalyst components, organoaluminum auxiliary catalysts, and organosilicon electron donors. The composition produces a catalyst system with a significantly higher crystallinity than (xylene) Less soluble) Polymer product provided by the previous catalyst as explained in the following comparative example • In addition, the catalyst system of the present invention using a specific conventional warp-shaped giglia-nata catalyst component, and Compared with other types of catalyst components, it provides better control of the xylene solubles of the polymer product. The paper size is applicable to the Chinese national standard (CNS > A4 specification (210X297 mm)! ^ — CI — ( (Please read the notes on the back and fill in this page)

、tT 6 經濟部中央樣隼局貝工消費合作社印製 A7 ___ B7_ 五、發明説明(4 ) 。此外’使用特定電子予體之本發明觸媒系統,與其他類 型之電子予體比較之下,對聚合物產物之二甲苯可溶物提 供較佳之控制。根據下文之本發明詳細說明及附帶實施例 ,可進一步明瞭此等及其他優點。 前述觸媒在與先前使用之電子予髖配對使用時,使聚 合物產物之結晶性較先前已知觸媒增加少許,但與本發明 所述之電子予體配對時,則大幅增加•本發明針對聚合物 性質(諸如二甲苯可溶物)提供改良之操作控制。 由 USP4,784,983 及 4,861 ,847 所述之觸媒與 CMDS,DIDS,DTDS,CPDS 及C I D S之組合物所得之最意外之結果,爲該觭媒系統 於丙烯聚合中所產生之聚合物之結晶性巨幅增高•該觸媒 系統顯然在介於4 — 200範園內之S i/Ti莫耳比下 ,達到髙於30kg/g — ca t · h之效率· 本發明亦提供一種聚合丙烯之方法•該方法包括: 藉著使經擔體化之吉格列-那塔觸媒成份與有機鋁化 合物接觸而形成觸媒,以三烷基鋁爲佳; 於與有機鋁接觸之同時或之後,使該觸媒與電子予體 接觸,該電子予體爲前述通式所述之有機矽化合物, 視情況地藉著使少量單體與觸媒接觸而使該觸媒預先 聚合; 將觸媒導入處於聚合條件下而含有單體之反應區內, 該區內視情況地含有額外量之有機鋁化合物及電子予體: 及 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨OX29?公釐〉 ! 、—- S ....... n I n i^rcί^· ..... I 1 n -I--、1T (請先«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裝 A7 __^_B7__ 五、發明説明(5 ) 取出聚合物產物。 若單體爲丙烯,則二甲苯可溶物介於0. 6— 3. OOwt%範園內,而反應區內之Si/Ti比例介 於4 一 2 0 0範圈內。若電子予體爲二環戊基二甲氧矽烷 ,而單體爲丙烯*則定義.爲聚合物產物之等規性(二甲苯 可溶物分率之五價物分佈百分比)之結晶性等於或大於 9 8%· 發明詳述 本發明有關一種充作電子予髏之特定化合物與用於使 丙烯聚合之特定觸媒之組合物· 已發現特定電子予體確實明顯地增進習用經擔體化吉 格列-那塔觸媒之催化性質•任何一種習用吉格列一那塔 過渡金屬化合物觸媒成份皆可用於本發明。電子予體一般 係根據兩種方式而用於形成吉格列一那塔觸媒及觸媒系統 •首先,當過渡金靥鹵化物與金雇氫化物或金屬烷基化物 反應時,內部電子予體可用於觸媒之形成反應中· 適於製備用吉格列一那塔觸媒成份之內部電子予體成 份有醚類,酮類,內酯類,具有N,P及/或S原子之電 子予體化合物及特定酯類。特別適用者有酞酸酯,諸如酞 酸二異丁酯,酞酸二辛酯,酞酸二苯酯及酞酸笮酯丁酯: 丙二酸酯,諸如丙二酸二異丁酯及丙二酸二乙酯;特戊酸 烷酯及特戊酸芳酯:馬來酸烷酯,馬來酸環烷酯及馬來酸 芳酯:碳酸烷酯及碳酸芳酯,諸如碳酸二異丁酯,碳酸乙 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇X:297公釐) CI — (請先蚶讀背面之注項再填寫本頁) 訂 A7 B7 五、發明説明(6 ) 苯酯及碳酸二苯酯;琥珀酸酯,諸如琥珀酸單乙酯及琥珀 酸二乙酯*此等酞酸酯爲較佳予體· 電子予體於觴媒系統中之第二種用途爲於聚合反應中 充作外來電子予體及立體調節劑•兩情況下可使用相同化 合物,但一般相異。一般外來電子予體爲有機矽化合物, 例如環己基甲基二甲氧矽烷(CMDS) ·兩種竃子予髖 之描述皆由USP4,535 * 068提供,其掲示在此 供作參考· 習用吉格列-那塔觭媒成份包含通式MR、之化合物 ,其中Μ爲金屬,R爲齒素或烴氧基,而X爲金屬價數。 Μ以過渡金屬爲佳,第I VB族,VB族或V I Β族金屬 更隹,而第I VB族金屬最隹,尤其是鈦· R以氣,溴, 烷氧基或苯氧基爲佳,氯或乙氣基更佳,而氣最佳。過渡 金屬化合物觸媒成份之說明實例有T i C 1 4, T 1 B r 4 * T i (0 C 2H 5 ) 3c 1, T i ( 0 c 2 H 5) 3C 1,T i (〇 c 3 Η 7 ) 2 C 1 2 * T i 0 C eH 13) 2 C 1 2,T i (0 c 2H s) 2 B Γ 2及 T i ( 0 c α 2h 2 5) C 1 3 · 可使用過渡金屬化合物之混 經濟部中央搮準局貝工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁) 合物。只要至少存有一種過渡金屬化合物,則對過渡金屬 化合物之數董不限制· 擔體應爲惰性固體,與習用吉格列一那塔觸媒之任何 一種成份皆爲化學惰性。擔體以鎂化合物爲佳。用以提供 用於觸媒成份之擔體來源之鎂化合物實例有鎂鹵化物,二 烷氧基鎂,烷氧基鎂鹵化物,鎂鹵氧化物,二烷基鎂,氧 本紙張尺度通用中國國家標準(CNS > A4規格(210X297公釐) 經濟部中夬揉準局貝工消費合作社印製 A7 ____B7_ 五、發明説明(7 ) 化鎂,氫氧化鎂,及鎂之羧酸鹽· 用爲輔觸媒之有機鋁化合物以通式A 5 R / 3之烷基 鋁爲佳,其中R ^爲具有由1 一 8個氮原子之烷基或鹵素 ,R >相同或相異,而至少一個R -爲烷基,R >相同或 相異•有機鋁化合物以烷基鋁,烷基鋁二鹵化物或二烷基 鋁鹵化物爲佳•烷基鋁以三烷基鋁最佳,諸如三乙基鋁( TEAJ2)或三異丁基鋁(ΤΙΒΑί)。 可用於本發明之一種特定吉格列一那塔觸媒成份爲用 於使烯烴聚合之市售吉格列-那塔觸媒成份,包含: 一種觸媒成份,基本上由約1. 5—6. 0重量%鈦 ,約10 - 20重置%鎂,約40 — 70重量%選自包括 氯,溴及碘之鹵基;約5 — 2 5重置%選自包括脂族,芳 族及脂環族多羧酸之酯類之多羧酸酯:及約0.1- 2. 5重童%選自包括磷酸及膦酸之烴酯之有機磷化合物 所組成,其中各烴基具有1個至6個碳原子,該觸媒成份 係藉著具有以下步揉之方法製備: a) 於溶劑混合物中溶解鎂齒化物化合物,以形成 均勻溶液,該鎂鹵化物選自包括鎂齒化物與水或醇之鎂鹵 化物錯合物及鎂鹵化物之衍生物*其中鹵原子被烴氧基或 鹵代烴氧基所取代;該溶劑混合物係由有機環氧化合物及 有機磷化合物所組成,以形成均匀溶液,該有機環氧化合 物選自包括脂族烴和二烯之氧化物,鹵化脂族烴及二烴之 氧化物及縮水甘油醚,皆具有2個至8個碳原子,而該有 機磷化合物則選自包括磷酸烷酯*磷酸芳酯,磷酸芳烷酯 本紙張尺度適用中國國家標準(CNS ) A4规格(210X297公釐) ' -10 - CI— (請讀背面之注意事項再填寫本頁) 訂 經濟部中央搮準局貝工消费合作社印輦 A7 B7 五、發明説明(8 ) ,亞磷酸烷酯,亞磷酸芳酯及亞磷酸芳烷酯,其中烷基具 有1個至4個碳原子,而芳基具有6倜至1 0個碳原子; b) 使該均勻溶液與具有通式 T i X „ ( 0 R ) 之液體鈦化合物混合,其中X爲鹵索 ,R爲相同或相異之烷基,而η爲〇至4之整數: c) 添加至少一種辅助沈澱劑,以形成沈澉物,其 選自包括羧酸酐,羧酸,醚及酮; d) 於出現沈澱物之時添加多羧酸酯: e) 自混合物分離沈澱物,使用鈦化合物 T i X „ ( 0 R ) 4_„或其混合物,於惰性稀釋劑中處理已 分離之沈澱物,其中X爲鹵素,R爲烴基而可相同或相異 ,且π爲由0至4之整數;及 f ) 使用有機惰性稀釋劑洗滌經處理之沈澱物,如 USP4,861,847 及 4,874,983 所揭示 ,該揭示於此供作參考· 用於形成觭媒之較佳辅助沈澉劑爲有機羧酸酐,以酞 酸酐更佳,添加置爲每莫耳鎂鹵化物有0. 03至1. 0 莫耳•較佳多羧酸酯選自包括芳族多羧酸之酯,以酞酸二 丁酯及酞酸二異丁酯爲佳·用於洗滌沈澱物之較佳情性稀 釋剤爲1 ,2 —二氣乙烷•適當之四鹵化鈦有Ti C l4 •TiBr^^Ti 14,而 TiCl4 較佳。 本發明特別有關一種外來電子予體,本發明所用之a 電子予體"一辭意指外來予體•外來電子予髖充作立體調 節劑,以控制所製聚合物之無規形式含置。亦可增加等規 本紙張尺度適用中國國家標準(CNS ) A4規格(210父297公釐.) ‘(請先M·讀背面之注意事項再填寫本頁) 訂 -11 - A7 B7 五、發明説明(9 ) 聚合物之產置•有機矽化合物已知於技藝界中作爲電子予 體•有機矽化合物電子予體實例係揭示於U S P 4,218,339;4,395-360: 4,328,122:4,473,660 及 4,927,797中•如前述者,特定觸媒於與特定電 子予髖配對時,可產生較隹結果·此種觸媒與電子予體配 對之實例揭示於USP4,562,173 ; 4,547,552;及 4,927,797 中· 電子予體具有通式S i Rm(OR / ) 4_m,其中R選 自包括烷基,環烷基,芳基及乙烯基;R"*爲烷基;而m 爲0 — 3,其中當R爲烷基時,R可與相同;當m爲 0,1或2時,基可相同或相異;而當m爲1,2或 3時,R基可相同或相異*電子予髖以選自具有下式之有 機矽化合物爲佳: OR, 經濟部中央標準局貝工消費合作社印製 (請先閏讀背面之注意事項再填寫本頁) 其中Rλ爲烷基或環烷基,含有鍵結於矽之一級,二級或 三級碳原子;R2及R3爲烷基或芳基:而爲烷基或環 烷基,具有鍵結於矽原子之二級或三級碳原子,尺^及 R4相同或相異,而R2及R 3相同或相異·於較佳具體實 例中,Ri爲具有3 — 5個碳原子而具有鏡像對稱性之二 本紙張尺度適用中國國家標準(CNS ) A4規格(210 X25»7公釐) -12 - 經濟部中央樣準局貝工消費合作社印裝 A7 B7 五、發明説明(10 ) k烷基:R 2及R 3爲甲基,乙基,丙基,或丁基,但非必 要相同:而爲具有3 — 6個碳原子而具有鏡像對稱性 之二級烷基或環烷基。R1々R4相同更佳,而爲環烷基, 尤其是具有5個碳原子之基團,即環戊基·特定電子予髖 有環己基甲基二甲氧矽烷(CMDS),二異丙基二甲氧 矽烷(D IDS),二第三丁基二甲氧矽烷(DTDS) ,二環戊基二甲氧矽烷(CPD S)及環己基異丙基二甲 氧矽烷(CIDS),以二環戊基二甲氧矽烷(CPDS )最佳。前述電子予釐與習用經擔體化吉格列一那塔觸媒 之組合物產生完全令人意外而凌越先前已知觸媒系統之結 果。本發明所述之電子予體可能受限於化合物安定性及操 作簡易性,包括儲存,運送及於工廠中之使用。 該觸媒系統可於宽幅S i/T i比例(4一2 00) 下達到高效果,而控制無規聚合物之形成,或將二甲苯可 溶物控制於相當低之檫準下,產生髙等規率。當其他觭媒 與前述電子予體配對時,聚合物產物之二甲苯可溶物直線 增髙•然而,使用特定經擔體化吉格列-那塔觸媒成份與 CMDS,DIDS,DTDS,CPDS 或 CIDS 之 本發明觸媒系統,當S i /T i比例由2 0 0降至4及更 低時,具有由約0. 6至約3. 0%之低二甲苯可溶物。 含有C P D S之觸媒系統亦於聚合物產物中提供較髙 之結晶性。聚合物產物之庚烷不溶物部分之中間五價物( mmmm)百分比極高,等於或大於9 7% · 本發明亦提供一種使丙烯聚合之方法,使用該觸媒及 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 1 I 11 ί I - — -«-I I - —— HI «n m (請$讀背面之注意事項再填寫本頁) -13 - A7 B7 五、發明説明(11 ) 前式所述之電子予體,其包括: a) 選擇習用經單髖化吉格列-那塔觸媒成份; b) 使該觸媒與有機鋁化合物接觸; c) 使該觸媒與前述電子予體接觸: d ) 將觸媒導入含有有機鋁化合物,電子予體及單 體之聚合反應區內;及 e) 自反應器取出聚合物產物· 經濟部中央橾準局負工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁) 雖然該觸媒系統可用於幾乎任何已知聚合方法中,然而較 佳之本發明方法包括使觸媒預聚,其係於觸媒與電子予® 接觸之後,藉著使少置之單舊與觸媒接觸而達成· U S P 4,769,935 及 4,927,797 描述一種預聚 方法,供作前文參考。如該揭示所述,提供用於觸媒之載 髖流,該觸媒與輔觸媒或有機鋁化合物接觸,該觸媒與電 子予體接觸,觸媒流與欲聚合之單體總置中之相當少置接 觴,觸媒流經管狀反應器,將已經預聚之觸媒和觸媒流導 入聚合反應區內*電子予體與輔觸媒同時地與觸媒接觸。 之後可自反應器取出電子予體。使用前述觸媒與前式所述 之電子予體時,觸媒可在反應中S i /T i莫耳比介於1 —10範匾內時*具有高於30kg/g — ca t ·1ι之 效率*聚合物產物亦可具有二甲苯可溶物介於2 -10wt%範圔內之特徵。 以下實施例及對照例將更詳細地說明本發明及其各種 優黏•結果列於表1 _ 2中·實施例所用之觸媒相信係使 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) • 14 - 經濟部中央標準局貝工消費合作社印製 A7 _B7_ 五、發明説明(12 ), TT 6 Printed by the Shellfish Consumer Cooperative of the Central Bureau of Samples of the Ministry of Economic Affairs A7 ___ B7_ V. Description of Invention (4). In addition, the catalyst system of the present invention using a specific electron donor provides better control of the xylene solubles of the polymer product compared to other types of electron donors. These and other advantages can be further understood from the following detailed description of the invention and the accompanying examples. When the aforementioned catalyst is used in combination with a previously used electron donor, the crystallinity of the polymer product is increased slightly compared with the previously known catalyst, but when it is paired with the electron donor described in the present invention, it is greatly increased. Provides improved operational control for polymer properties such as xylene solubles. The most unexpected result obtained from the catalysts described in USP 4,784,983 and 4,861,847 and the composition of CMDS, DIDS, DTDS, CPDS and CIDS is the polymerization of the catalyst system in the polymerization of propylene. The crystallinity of the material is greatly increased. The catalyst system obviously achieves an efficiency of 30 kg / g-ca t · h at a Si / Ti molar ratio between 4 and 200 yuan. The present invention also provides A method for polymerizing propylene. The method includes: forming a catalyst by contacting a supported Gigliole-Natta catalyst component with an organoaluminum compound, preferably trialkylaluminum; contacting with organoaluminum At the same time or after, the catalyst is brought into contact with an electron donor, which is an organosilicon compound described in the aforementioned general formula, and the catalyst is polymerized in advance by contacting a small amount of monomer with the catalyst as appropriate. The catalyst is introduced into a reaction zone containing monomers under polymerization conditions, and the zone contains additional amounts of organoaluminum compounds and electron donors as appropriate: and this paper size applies Chinese National Standard (CNS) A4 specifications ( 2 丨 OX29? Mm>!, --- S ....... n I ni ^ rcί ^ · ..... I 1 n -I--, 1T (Please read «Read the precautions on the back before filling out this page) Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 __ ^ _ B7__ 5 5. Description of the invention (5) Take out the polymer product. If the monomer is propylene, the xylene solubles are between 0.6 and 3. OOwt% in Fanyuan, and the Si / Ti ratio in the reaction zone is between 4 and 1. Within the range of 2000. If the electron donor is dicyclopentyldimethoxysilane and the monomer is propylene *, it is defined as the isotacticity of the polymer product (pentavalent of xylene soluble fraction Distribution percentage) has a crystallinity equal to or greater than 98%. DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a composition of a specific compound acting as an electron donor and a specific catalyst for polymerizing propylene. It has been found that the specific electron donor is indeed obvious. To enhance the catalytic properties of conventional Giggle-Natta catalysts • Any conventional Giglie-Natta transition metal compound catalyst component can be used in the present invention. Electron donors are generally based on two methods. Used to form Giglia-Nata catalysts and catalyst systems. • First, when When hydride or metal alkylate is used for reaction, the internal electron donor can be used in the formation reaction of the catalyst. The internal electron donor components suitable for the preparation of Giglia-Nata catalyst components include ethers and ketones. Lactones, electron donor compounds with N, P and / or S atoms and specific esters. Particularly suitable are phthalates, such as diisobutyl phthalate, dioctyl phthalate, diphenyl phthalate And butyl phthalate: malonates such as diisobutyl malonate and diethyl malonate; alkyl pivalate and aryl pivalate: alkyl maleate, maleic acid Naphthenates and aryl maleates: Alkyl carbonates and aryl carbonates, such as diisobutyl carbonate, ethyl carbonate. Paper size is subject to Chinese National Standard (CNS) A4 specifications (21 ×: 297 mm) CI — (Please read the notes on the back before filling this page) Order A7 B7 V. Description of the invention (6) Phenyl ester and diphenyl carbonate; Succinate esters, such as monoethyl succinate and diethyl succinate * Isophthalates are the preferred donors. The second use of electron donors in rhenium systems is as foreign electron donors in polymerization reactions. • modulator and the stereoscopic two cases may be the same compound, but generally different. Generally, the foreign electron donor is an organosilicon compound, such as cyclohexylmethyldimethoxysilane (CMDS). · The descriptions of the two types of gardenia are given by USP4,535 * 068, and the details are shown here for reference. The Gle-Natta hydrazone component includes compounds of the general formula MR, where M is a metal, R is a halide or a hydrocarbyloxy group, and X is a metal valence. M is preferably a transition metal. Groups I VB, VB, or VI B are more 隹, and group I VB is the most 隹, especially titanium. R is preferably gas, bromine, alkoxy, or phenoxy. Chlorine or ethyl gas is better, and gas is the best. Examples of transition metal compound catalyst components are T i C 1 4, T 1 B r 4 * T i (0 C 2H 5) 3c 1, T i (0 c 2 H 5) 3C 1, T i (〇c 3 Η 7) 2 C 1 2 * T i 0 C eH 13) 2 C 1 2 , T i (0 c 2H s) 2 B Γ 2 and T i (0 c α 2h 2 5) C 1 3 · Available Printed by Shelley Consumer Cooperative, Central Bureau of Standards and Quarantine, Ministry of Mixed Economics of Transition Metal Compounds (please read the precautions on the back before filling this page). As long as there is at least one transition metal compound, the number of transition metal compounds is not limited. The support should be an inert solid, and any one of the components of the conventional Giglia-Nata catalyst is chemically inert. The support is preferably a magnesium compound. Examples of magnesium compounds used to provide a support source for catalyst ingredients are magnesium halides, dialkoxy magnesium, alkoxy magnesium halides, magnesium halides, dialkyl magnesium, oxygen. National Standard (CNS > A4 Specification (210X297mm) Printed by A7 of the Ministry of Economic Affairs, Zhuhai Bureau of Shellfish Consumer Cooperatives __B7_ V. Description of the Invention (7) Magnesium Oxide, Magnesium Hydroxide, and Magnesium Carboxylate · Use The organoaluminum compound as the auxiliary catalyst is preferably an alkyl aluminum of the general formula A 5 R / 3, wherein R ^ is an alkyl or halogen having 1 to 8 nitrogen atoms, and R > same or different, and At least one R-is an alkyl group, and R > same or different. The organoaluminum compound is preferably an alkyl aluminum, an alkyl aluminum dihalide or a dialkyl aluminum halide. The alkyl aluminum is preferably a trialkyl aluminum. , Such as triethylaluminum (TEAJ2) or triisobutylaluminum (ΤΙΒΑί). A specific giglia-nata catalyst component that can be used in the present invention is a commercially available giglia-nata for polymerizing olefins. Catalyst component, including: A catalyst component, consisting essentially of about 1.5-6. 0 wt% titanium, about 10-20% reset About 40-70% by weight are selected from halogen groups including chlorine, bromine and iodine; about 5-2 5% by weight are selected from polycarboxylic acid esters including aliphatic, aromatic and alicyclic polycarboxylic acid esters : And about 0.1-2.5% by weight are selected from organic phosphorus compounds including hydrocarbon esters of phosphoric acid and phosphonic acid, wherein each hydrocarbon group has 1 to 6 carbon atoms, and the catalyst component has the following steps Preparation by kneading method: a) Dissolving a magnesium halide compound in a solvent mixture to form a homogeneous solution, the magnesium halide is selected from the group consisting of a magnesium halide complex of magnesium dentate and water or an alcohol, and a derivative of a magnesium halide * Wherein the halogen atom is replaced by a alkoxy group or a halogenated alkoxy group; the solvent mixture is composed of an organic epoxy compound and an organic phosphorus compound to form a uniform solution, the organic epoxy compound is selected from the group consisting of aliphatic hydrocarbons and Diene oxides, halogenated aliphatic hydrocarbons and dihydrocarbon oxides and glycidyl ethers all have 2 to 8 carbon atoms, and the organic phosphorus compound is selected from the group consisting of alkyl phosphates * aryl phosphates, aryl phosphates Alkyl ester This paper is applicable to Chinese National Standard (CNS) A 4 Specifications (210X297 mm) '-10-CI— (Please read the notes on the back and fill in this page) Order the Ai B7 of the Beijin Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 5. Description of the invention (8), Phosphorous acid Alkyl esters, aryl phosphites and aralkyl phosphites, in which the alkyl group has 1 to 4 carbon atoms, and the aryl group has 6 to 10 carbon atoms; b) the homogeneous solution has a general formula T i X „(0 R) is a mixture of liquid titanium compounds, where X is halosol, R is the same or different alkyl group, and η is an integer from 0 to 4: c) Add at least one auxiliary precipitant to form a precipitate A compound selected from the group consisting of carboxylic anhydrides, carboxylic acids, ethers and ketones; d) adding a polycarboxylic acid ester when a precipitate appears: e) separating the precipitate from the mixture, using a titanium compound T i X (0 R) 4_ „or a mixture thereof, treating the separated precipitate in an inert diluent, wherein X is halogen, R is a hydrocarbon group and may be the same or different, and π is an integer from 0 to 4; and f) using organic inert dilution Agent to wash the treated precipitate, as disclosed in USP 4,861,847 and 4,874,983, which is disclosed here For reference · The preferred auxiliary precipitation agent for the formation of rhenium is organic carboxylic anhydride, more preferably phthalic anhydride, and the addition is set to 0.03 to 1.0 mole per mole of magnesium halide. The acid ester is selected from the group consisting of aromatic polycarboxylic acid esters, preferably dibutyl phthalate and diisobutyl phthalate. • Better emotional dilution for washing precipitates. 1,2 digasethane. • Suitable titanium tetrahalides are Ti C l4 • TiBr ^^ Ti 14 and TiCl4 is preferred. The present invention is particularly related to a foreign electron donor. The term "a electron donor" used in the present invention means "external donors". Foreign electrons are used as stereoregulators to control the random form of the polymer produced. . Can also increase isotactic paper size Applicable to Chinese National Standards (CNS) A4 specifications (210 mm 297 mm.) '(Please read the notes on the back before filling this page) Order-11-A7 B7 V. Invention Explanation (9) Production of polymers • Organic silicon compounds are known in the art world as electron donors • Examples of electron donors for organic silicon compounds are disclosed in USP 4,218,339; 4,395-360: 4,328 , 122: 4,473,660 and 4,927,797 • As mentioned above, specific catalysts can produce better results when paired with specific electron donors. Examples of such catalysts paired with electron donors are revealed In USP 4,562,173; 4,547,552; and 4,927,797 · The electron donor has the general formula S i Rm (OR /) 4_m, where R is selected from the group consisting of alkyl, cycloalkyl, and aryl And vinyl; R " * is an alkyl group; and m is 0-3, wherein when R is an alkyl group, R may be the same; when m is 0, 1, or 2, the groups may be the same or different; and when When m is 1, 2, or 3, the R groups may be the same or different. * The electrons are preferably selected from organosilicon compounds having the formula: OR, printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. (Please read the notes on the back before filling out this page) where Rλ is an alkyl or cycloalkyl group, which contains the first, second or third carbon atoms bonded to silicon; R2 and R3 are alkyl or aryl groups: Alkyl or cycloalkyl, having secondary or tertiary carbon atoms bonded to a silicon atom, and R4 and R4 are the same or different, and R2 and R3 are the same or different. In a preferred embodiment, Ri is the second paper with 3 to 5 carbon atoms and mirror symmetry. Applicable to China National Standard (CNS) A4 specification (210 X25 »7 mm). Packing A7 B7 V. Description of the invention (10) k alkyl: R 2 and R 3 are methyl, ethyl, propyl, or butyl, but not necessarily the same: but have a mirror image with 3 to 6 carbon atoms Symmetric secondary alkyl or cycloalkyl. R1々R4 are the same and better, but are cycloalkyl, especially the group with 5 carbon atoms, that is, cyclopentyl. Specific electrons to the hip are cyclohexylmethyldimethoxysilane (CMDS), diisopropyl Dimethoxysilane (D IDS), di-tertiary butyldimethoxysilane (DTDS), dicyclopentyldimethoxysilane (CPD S) and cyclohexyl isopropyldimethoxysilane (CIDS). Cyclopentyldimethoxysilane (CPDS) is the best. The combination of the aforementioned electronic pretreatment and the conventionally-supported Giglia-Nata catalyst produced completely unexpected results that surpass previously known catalyst systems. The electron donor of the present invention may be limited by the stability and ease of operation of the compound, including storage, transportation, and use in a factory. The catalyst system can achieve a high effect at a wide S i / T i ratio (4 to 2 00), and control the formation of random polymers, or control the xylene solubles to a relatively low level. Generates isotacticity. When other catalysts are paired with the aforementioned electron donors, the xylene solubles of the polymer product increase linearly. However, the use of specific supported Giglia-Natta catalyst components with CMDS, DIDS, DTDS, CPDS Or the catalyst system of the present invention of CIDS, when the S i / T i ratio is reduced from 200 to 4 and lower, has a low xylene solubles from about 0.6 to about 3.0%. The catalyst system containing C P D S also provides relatively high crystallinity in the polymer product. The percentage of intermediate pentavalents (mmmm) in the heptane insoluble portion of the polymer product is extremely high, equal to or greater than 9 7%. The present invention also provides a method for polymerizing propylene. The use of the catalyst and the paper size are applicable to China Standard (CNS) A4 specification (210X297 mm) 1 I 11 ί I-—-«-II-—— HI« nm (Please read the notes on the back and fill in this page) -13-A7 B7 V. Description of the invention (11) The electron donor described in the foregoing formula, which includes: a) selecting a conventional single-gilled Giglia-Natta catalyst component; b) bringing the catalyst into contact with an organoaluminum compound; c) bringing the catalyst into contact The medium is in contact with the aforementioned electron donor: d) the catalyst is introduced into the polymerization reaction zone containing the organoaluminum compound, the electron donor and the monomer; and e) the polymer product is taken out of the reactor. Printed by a consumer cooperative (please read the notes on the back before filling out this page) Although the catalyst system can be used in almost any known polymerization method, the preferred method of the present invention involves pre-polymerizing the catalyst, which is based on the catalyst After contacting E-Yu®, The old contact with the catalyst was reached. U S P 4,769,935 and 4,927,797 describe a pre-polymerization method for the previous reference. As described in the disclosure, a hip flow for a catalyst is provided, the catalyst is in contact with an auxiliary catalyst or an organoaluminum compound, the catalyst is in contact with an electron pre-cursor, and the catalyst stream is integrated with a monomer to be polymerized. A relatively small number of contacts are placed, and the catalyst flows through the tubular reactor, and the pre-polymerized catalyst and the catalyst flow are introduced into the polymerization reaction zone. The electron precursor and the auxiliary catalyst are simultaneously contacted with the catalyst. The electron donor can then be removed from the reactor. When using the aforementioned catalyst and the electron donor described in the previous formula, the catalyst can have a S i / T i mole ratio between 1 and 10 van plaques in the reaction * with a higher than 30 kg / g — ca t · 1ι Efficiency * The polymer product can also be characterized by xylene solubles in the range of 2-10 wt%. The following examples and comparative examples will explain the present invention and its various advantages in more detail. • The results are listed in Tables 1 and 2. The catalysts used in the examples are believed to make this paper scale applicable to the Chinese National Standard (CNS) A4 specification ( 210X297 mm) • 14-Printed A7 _B7_ by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (12)

用 USP4,861,847 及 4 * 784,983 所掲 示之材料及方法製備,Catalyst Resources所販售之商標 爲| Lynx 1000〃 。對照例所用之觸媒相信係使用USP 4,927,797;4,816,433 及 4,839,321所揭示之材料及方法製備,Toho Titanium, Inc.販售商標爲、丁11(:-3 2八,· 實施例1 於進行聚合之前,藉著於無水氮之固定排氣下,加熱 至高於1 0 0°C之溫度歷經最少3 0分鐘*而自反應器排 除任何微置之濕氣及空氣•加熱之後,於氮下將反應器冷 卻至室溫(25 eC) ·反應器於室溫下安定化,之後添加 32mmoJ?氫及1. 45)2丙烯•反應器於 1 3 00 r pm下攪拌,而溫度上升至70 X·於 40cc管式反應器中添加1. Ommoi TEA又及 0. lmmo又環己基甲基二甲氧矽烷(CMDS) ·使 TE AP及予體預先接觸約1分鐘*於4 0 c c反應简中 添加1 0毫克觸媒於磺油中之懸浮液。使觸媒與TEAj? 和予體混合物預先接觸約2分鐘》管式反應器聯接於反應 器之入口點,填入室溫液髏丙烯,使之聚合約5秒鐘,以 進行觸媒之預聚。將容器之內容物沖入含有1. 45L室Prepared using the materials and methods shown in USP4, 861, 847 and 4 * 784, 983. Trademarks sold by Catalyst Resources are | Lynx 1000〃. The catalyst used in the comparative example is believed to be prepared using the materials and methods disclosed in USP 4,927,797; 4,816,433 and 4,839,321. Toho Titanium, Inc. sells the trademarks as Ding 11 (:- 3 2/8, Example 1 Prior to the polymerization, by heating under a fixed exhaust gas of anhydrous nitrogen to a temperature higher than 100 ° C for a minimum of 30 minutes *, any micro-moisture was excluded from the reactor. Air and air • After heating, cool the reactor to room temperature (25 eC) under nitrogen. • Stabilize the reactor at room temperature, then add 32mmoJ? Hydrogen and 1. 45) 2 propylene • reactor at 1 3 00 Stir at pm, and the temperature rises to 70 X. Add 1. Ommoi TEA and 0.1 lmmo and cyclohexylmethyldimethoxysilane (CMDS) to the 40cc tube reactor. Make TE AP and the pre-contact in advance. About 1 minute * Add 10 mg of the catalyst to a suspension of sulphur oil in the 40 cc reaction brief. The catalyst is brought into contact with TEAj? And the precursor mixture for about 2 minutes in advance. The tubular reactor is connected to the inlet of the reactor, filled with liquid propylene at room temperature, and allowed to polymerize for about 5 seconds to perform catalyst pre-treatment. Get together. Pour the contents of the container into a chamber containing 1.45L

溫丙烯之反應器內。反應器中液髖丙烯之總置約2. 9L •聚合反應進行1小時,此時藉著排除過置丙烯並使反應 器冷卻至室溫而終止反應· 本紙張尺度適用中國國家揉準(CNS ) A4規格(210X297公釐} r------r装-11 (請先閲讀背面之注意事項再填寫本頁) 訂 -15 - A7 B7 五、發明説明(l3 ) 開啓反應器以收集聚合物產物,將彼乾燥,稱重並分 析•由所用之電子予體之莫耳數置除以觸媒之莫耳數置計 算S i/T i莫耳比·將聚合物溶於熱二甲苯中,將溶液 冷卻至0°C,使等規形式沈澱,而測定二甲苯可溶物。二 甲苯可溶物爲可溶於冷二甲苯中之聚合物的% t % ·藉 NMR分析測定五價物分佈·將聚合物絮狀物溶於沸騰之 二甲苯中’之後於攪下,將二甲苯溶液逐滴添加於甲酵中 ’使聚合物於甲醉中沈澱•濾出沈澱物,以沸騰之庚烷萃 取隔夜•結果列於表1。 I表-|_ (請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裝 聚合條件概略表 觸媒重量: 10. 0毫克 TEA1用置(輔觸媒): 1.0毫莫耳 CMDS用1:(電子予髖): 0. 1毫莫耳 Al/Ti: 200 Al/Si: 10 Si/Ti: 20 氫: 240 Δ ps i g 丙烯: 2.9L(1500g) 溫度: 7 0°C 時間: 1小時 實施例2 — 9 重複實例1之方法,不同處係CMD S之總置如表1 訂 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨0X297公釐) -16 - A7 B7 五、發明説明(l4) 所示般地由1毫莫耳變成〇. 002毫莫耳•結果列於表 1 · 實施例10-15 重複實例1之方法,不同處係使用二異丙基二甲氧矽 烷(DIDS)取代CMDS,而DIDS總量如表1所 示般地由2毫莫耳變成〇. 〇〇33毫莫耳。結果列於表 1 · 實施例16-18 重複實例1之方法,不同處係使用二第三丁基二甲氧 矽烷(DTDS)取代CMDS,而DTDS之總置如表 1所示般地由2奄莫耳變成〇. 〇5毫莫耳·結果列於表 1 · 實施例1 9 一 2 4 重複表1之方法,不同處係使用二環戊基二甲氧矽烷 (CPDS)取代CMDS,而CPDS總1:如表1所示 般地由2毫莫耳變成〇. 0033毫莫耳•結果列於表1 〇 實施例25-30 重複實例1之方法,不同處係使用環己基異丙基二甲 氧矽烷(C I DS)取代CMDS,而C I DS之總量如 本紙浪尺度適用t國國家梂準(CNS )八4规格(2I0X297公釐) 1._. 1 丨|C衣—I (請先聞讀背面之注意事項再填寫本頁) 訂 經濟部中央樣準局負工消费合作社印装 -17 - A7 B7 五、發明説明(15 ) 表1所示般地由2奄莫耳變成0 列於表1。 0033毫莫耳•結果 對照例1 一 3 0 重複實例1方法,不同處係使用其他市售吉格列-那 塔觸媒成份取代實例1 - 3 0所用之觸媒成份•結果列於 表2 · 表1 實施TEA1 CMDS 觸媒產量二甲苯可等規性 Μ_ mmol mmol A 1 /Si 〇Lg__S_ 溶物-,“mmm 1 1 2 0.5 1 0 5 1 3. 0 經濟部中央梂準局負工消費合作社印裝 2 3 4 5 6 7 8 9 10 11 12 13 1 1 1 1 1 1 1 1 0. 5 2.0 0.1 10 0. 05 20 0.033 30 0.02 50 0.01 100 0.002 500 DIPS 2 0.5 1 1.0 0.5 2. 00.1 10 10 10 10 10 10 10 10 10 10 10 10 10 51.4 2.3 102 1.4 195 1.7 216 2.0 172 269 234 124 101 133 204 278 3.2 2.3 5.1 23.70.81.1 1. 2 1.6 ---I —----------訂 (請先聞讀背面之注意事項再填寫本頁) 96 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) _ 18 _ A7 B7 經濟部中央標準局貝工消費合作社印裝 L、 14 發明説明 1 (16 ) 0.05 20 10 223 2.8 15 1 0. 033 30 10 225 2. 1 DTDS 16 1 2 0.5 10 208 1.4 17 1 1 1.0 10 246 1.6 18 1 0.5 2.0 10 195 1.5 CPDS 19 1 2 0.5 10 105 1.1 98. 4 20 1 1 1.0 10 136 1.0 9 8.4 21 1 0.5 2.0 10 210 0. 9 97.9 22 1 0. 1 10 10 260 0. 9 98. 5 23 1 0.05 20 10 315 0. 6 24 1 0.033 30 10 249 0. 6 98.5 CTDS 25 1 2 0.5 10 70 0.9 98. 4 26 1 1 1.0 10 127 0.9 27 1 0. 5 2.0 10 181 0.9 28 1 0.1 10 10 119 1.6 29 1 0.05 20 10 134 2.0 30 1 0.033 30 10 157 2.4Inside the reactor of warm propylene. The total amount of liquid propylene in the reactor was about 2.9L. The polymerization reaction was carried out for 1 hour. At this time, the reaction was terminated by removing the excess propylene and allowing the reactor to cool to room temperature. ) A4 size (210X297 mm) r ------ r pack -11 (Please read the precautions on the back before filling this page) Order -15-A7 B7 V. Description of the invention (l3) Open the reactor to collect Polymer product, dried, weighed and analyzed • Calculate S i / T i molar ratio by dividing the Mohr number of the electron donor used by the Mohr number of the catalyst. • Dissolve the polymer in heat. In toluene, the solution was cooled to 0 ° C to precipitate isotactic form, and the xylene solubles were measured. The xylene solubles are% t% of the polymer soluble in cold xylene. Pentavalent distribution: Dissolve the polymer floc in boiling xylene, and then add the xylene solution dropwise to the formazan with stirring. The polymer precipitates in the intoxicant. Filter out the precipitate. Overnight extraction with boiling heptane • Results are shown in Table 1. Table I-| _ (Please read the notes on the back and fill out this page) Summary of the polymerization conditions printed by the Shell Standard Consumer Cooperative of the Central Bureau of Standards of the Ministry of Catalysts Weight of the catalyst: 10. 0 mg for TEA1 (auxiliary catalyst): 1.0 millimolar for CMDS 1: (electronic to hip): 0.1 millimeter Mohr Al / Ti: 200 Al / Si: 10 Si / Ti: 20 Hydrogen: 240 Δ ps ig Propylene: 2.9L (1500g) Temperature: 70 ° C Time: 1 hour Example 2-9 Repeat the method of Example 1 The general arrangement of CMD S in different places is as shown in Table 1. The paper size of the revised paper is applicable to the Chinese National Standard (CNS) A4 specification (2 丨 0X297 mm) -16-A7 B7 V. The description of the invention (l4) consists of 1 Millimoles became 0.002 millimoles. The results are shown in Table 1. Example 10-15 The method of Example 1 was repeated, except that CMDS was replaced by diisopropyldimethoxysilane (DIDS), and the total amount of DIDS As shown in Table 1, it changed from 2 millimoles to 0.003 millimoles. The results are shown in Table 1. Example 16-18 The method of Example 1 was repeated, except that the second and third butyl dimethyl groups were used. Oxysilane (DTDS) replaced CMDS, and the total set of DTDS was changed from 2 mol to 0.5 mol as shown in Table 1. Results are shown in Table 1. Example 1 9 2 4 Repeat the method of Table 1, except that CMDS is replaced by dicyclopentyldimethoxysilane (CPDS), and the total CPDS is 1: from 2 millimoles to 0.033 millimoles as shown in Table 1. • The results are shown in Table 10. Examples 25-30 The method of Example 1 was repeated, except that cyclohexyl isopropyl dimethoxysilane (CI DS) was used instead of CMDS, and the total amount of CI DS was the same as the standard of this paper. T China National Standards (CNS) 8 4 specifications (2I0X297 mm) 1._. 1 丨 | C clothing—I (please read the precautions on the back before filling out this page). Cooperative printed -17-A7 B7 V. Description of the invention (15) Table 1 changes from 2 奄 moles to 0 as shown in Table 1. 0033 millimolars • Results Comparative Example 1 to 3 0 The method of Example 1 was repeated, except that other commercially available Giglia-Nata catalyst components were used instead of the catalyst components used in Examples 1 to 30. The results are shown in Table 2. · Table 1 Implementation of TEA1 CMDS Catalyst Yield Xylene Isotacticity M_mmol mmol A 1 / Si 〇Lg__S_ Soluble-, "mmm 1 1 2 0.5 1 0 5 1 3. 0 Co-operative print 2 3 4 5 6 7 8 9 10 11 12 13 1 1 1 1 1 1 1 1 0.5. 2.0 0.1 10 0. 05 20 0.033 30 0.02 50 0.01 100 0.002 500 DIPS 2 0.5 1 1.0 0.5 2. 00.1 10 10 10 10 10 10 10 10 10 10 10 10 10 51.4 2.3 102 1.4 195 1.7 216 2.0 172 269 234 124 101 133 204 278 3.2 2.3 5.1 23.70.81.1 1. 2 1.6 --- I -------- ---- Order (please read the precautions on the back before filling this page) 96 This paper size applies to Chinese National Standard (CNS) A4 (210X297 mm) _ 18 _ A7 B7 Shellfish Consumption of Central Standards Bureau, Ministry of Economic Affairs Cooperative printed L, 14 Description of invention 1 (16) 0.05 20 10 223 2.8 15 1 0. 033 30 10 225 2. 1 DTDS 16 1 2 0.5 10 208 1.4 17 1 1 1.0 10 246 1.6 18 1 0.5 2.0 10 195 1.5 CPDS 19 1 2 0.5 10 105 1.1 98. 4 20 1 1 1.0 10 136 1.0 9 8.4 21 1 0.5 2.0 10 210 0. 9 97.9 22 1 0. 1 10 10 260 0. 9 98. 5 23 1 0.05 20 10 315 0. 6 24 1 0.033 30 10 249 0. 6 98.5 CTDS 25 1 2 0.5 10 70 0.9 98. 4 26 1 1 1.0 10 127 0.9 27 1 0. 5 2.0 10 181 0.9 28 1 0.1 10 10 119 1.6 29 1 0.05 20 10 134 2.0 30 1 0.033 30 10 157 2.4

Mu - - -- n^i I- 8-- - -I— i ----- I ii · 1- I 1· - - I - - - i ml :二|·- 一eJ -(請先閲讀背面之注意i項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -19 - 附件2 :第 85112303 號專利申請案 中文說明書修正頁 民國88年f月修正 五、發明說明(17) 經濟部智慧財產局員工消費合作社印製Mu---n ^ i I- 8----I— i ----- I ii · 1- I 1 ·--I---i ml: two | ·-one eJ-(please first Read the note on the back of the page and fill in this page) This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) -19-Attachment 2: Amendment page of Chinese specification of Patent Application No. 85112303 V. Description of the invention (17) Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs

對照 TEA1 CMDS 例 mmol mmol 1 1 2 2 1 1 3 1 0.5 4 1 0.1 5 1 0.05 6 1 0.033 7 1 0.02 8 1 0.01 g 1 0.002 PIPS 10 1 2 11 1 1 12 1 0.5 13 1 0.1 14 1 0.05 15 1 0.033 ptps 16 1 «0 2 17 1 1 18 1 0. 5 CPDS A1 /Si 表2 觸媒 m or 產量 β _ 0.5 10 48 1. 0 10 142 2. 0 10 205 10 10 269 20 10 249 30 10 269 50 10 280 100 10 302 500 10 294 0.5 10 163 1.0 10 214 2.0 10 294 10 10 305 20 10 249 30 10 243 0.5 10 274 1.0 10 246 2.0 10 309 B8QS〇msL·,Λ 日— 補炙 二甲苯可 等規性 溶物.wt% % in m τη m 4.1 0.9 1.5 1.4 95 2.8 7.1 8.7 6.8 93.6 15. 7 91. 6 2.9 92.2 3.1 95 2.9 96 2.4 2.5 2-8 3.9 3.1 96 3.7 (請先閱讀背面之注意事項再填寫本頁) -^fv '裝--------訂----- 本紙張尺度適用中國國家標準(CNS)A4規格(210x297公芨) -20 - 五、 發明説明(18 ) 19 1 2 0. 5 10 20 1 1 1. 0 10 21 1 0. 5 2.0 10 22 1 0.1 10 10 23 1 0.05 20 10 24 1 0. 033 30 10 CIDS 25 1 2 0. 5 10 26 1 1 1.0 10 27 1 0.5 2.0 10 28 1 0.1 10 10 29 1 0. 05 20 10 30 1 0.033 30 10 (請奋讀背面之注意^項再填寫本筲) 订 經濟部中央揉準局貝工消费合作社印製 聚丙烯之結晶性由立髖 及無規聚合物 或庚烷不溶物部分隨著二甲 述數據所示,特定電子予體 當少ft之二甲苯可溶物•使 P D S時,可增強此種現象 如前述資施例表1及2 _ 2 7及表1之特定觸媒成 與對照例1一2 7及表2之 明顯較低*如實施例16_ A7 B7 140 2, 9 97. 9 209 3. 1 281 2. 9 96. 6 1 294 2. 4 346 2. 5 307 2. 8 97.7 98 2. 4 195 1. 8 237 2. 0 267 2. 3 206 2. 4 224 2. 4 規則性( 即 等 規性( 含置控制 • 通 f ~" Γ|3 甲苯 及/ 苯可溶物 之 減 少而增 加, 如前 與特定觸 媒 成 份組合 ,產 生相 用特定觸 媒 成 份之同 時使 用C 所示,各 電 子 予證與 實施 例1 份之組合 物 之 二甲苯 可溶 物, 相同電子 予 體 相較之 下, 通常 2 1及表 1 和 2所示 ,如 所描 本紙張尺度通用中國國家標準(CNS ) A4規格(210X297公釐) -21 - A7 B7 五、發明説明(19 ) 述般地使用C P D S與觸媒成份時,產生相對二甲苯可溶 物最低,而相對結晶性最高之丙烯。前述C P D S與觸媒 成份之組合物具有髙於其他電子予體與該觸媒成份之組合 物之活性· '(請先閲讀背面之注意事項再填寫本頁) 經濟部中央橾準局黄工消费合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210 X297公釐) -22 -Control TEA1 CMDS Example mmol mmol 1 1 2 2 1 1 3 1 0.5 4 1 0.1 5 1 0.05 6 1 0.033 7 1 0.02 8 1 0.01 g 1 0.002 PIPS 10 1 2 11 1 1 12 1 0.5 13 1 0.1 14 1 0.05 15 1 0.033 ptps 16 1 «0 2 17 1 1 18 1 0. 5 CPDS A1 / Si Table 2 Catalyst m or output β _ 0.5 10 48 1. 0 10 142 2. 0 10 205 10 10 269 20 10 249 30 10 269 50 10 280 100 10 302 500 10 294 0.5 10 163 1.0 10 214 2.0 10 294 10 10 305 20 10 249 30 10 243 0.5 10 274 1.0 10 246 2.0 10 309 B8QS〇msL ·, Λ day — supplemental xylene Isotactic solution.wt%% in m τη m 4.1 0.9 1.5 1.4 95 2.8 7.1 8.7 6.8 93.6 15. 7 91. 6 2.9 92.2 3.1 95 2.9 96 2.4 2.5 2-8 3.9 3.1 96 3.7 (Please read the Please fill in this page for the matters needing attention)-^ fv 'Packing -------- Order ----- This paper size is applicable to China National Standard (CNS) A4 (210x297 cm) -20-V. Description of the invention (18) 19 1 2 0. 5 10 20 1 1 1. 0 10 21 1 0. 5 2.0 10 22 1 0.1 10 10 23 1 0.05 20 10 24 1 0. 033 30 10 CIDS 25 1 2 0. 5 10 26 1 1 1. 0 10 27 1 0.5 2.0 10 28 1 0.1 10 10 29 1 0. 05 20 10 30 1 0.033 30 10 (please read the notes on the back ^ and fill in this note) Order the seal of the Shellfish Consumer Cooperative of the Central Bureau of the Ministry of Economic Affairs The crystallinity of polypropylene is determined by standing hips and random polymers or heptane insolubles. As shown in the dimethyl data, specific electron donors are less ft of xylene solubles. • When PDS is used, this can be enhanced. This phenomenon is as shown in Tables 1 and 2 _ 2 7 and Table 1 and the specific catalyst composition of Table 1 is significantly lower than that of Comparative Examples 1 2 7 and Table 2 * As in Example 16_ A7 B7 140 2, 9 97. 9 209 3. 1 281 2. 9 96. 6 1 294 2. 4 346 2. 5 307 2. 8 97.7 98 2. 4 195 1. 8 237 2. 0 267 2. 3 206 2. 4 224 2. 4 Rules (Isotacticity) (Including control • Through f ~ " Γ | 3 Toluene and / benzene solubles decrease and increase, as before, combined with specific catalyst components to produce compatible specific catalyst components for simultaneous use As shown in C, each electron certificate is compared with the xylene-soluble material of the composition of Example 1 in the same electron donor. Below, usually 2 1 and Tables 1 and 2, as described in the paper size common Chinese National Standard (CNS) A4 specifications (210X297 mm) -21-A7 B7 V. Use the CPDS as described in the description of the invention (19) When used with catalyst components, it produces propylene with the lowest relative xylene solubles and the highest relative crystallinity. The aforesaid composition of CPDS and catalyst component has the activity of other electronic donors and the composition of the catalyst component. "(Please read the precautions on the back before filling this page) The paper size printed by the cooperative is applicable to the Chinese National Standard (CNS) A4 (210 X297 mm) -22-

Claims (1)

附件3(a) 第851 12303 號專利申請案 中文比較數據 民國88年f月呈Annex 3 (a) Patent Application No. 851 12303 Chinese Comparative Data 6 a L 必 w寸 96 εΜ τ19 9Π Τ3ΜΜ ^n^^^^^fr丨 . 担蹈她 £傾請委員明示,本案修正後是否變更原實質内- ϋ:0' g·00' Δ·10!: CN OJ LO VO σ> σ\ \D0> Lrn69^65Δ6 σ» h in co οϊ n (n oj oa οι σ» h卜 cn m cn c\ r-i σ\ in co <N r> (N CM 03 <N OrHOJfO 寸 in vo r- co rH rH Η «Η, rH «—I «Η «—I «Η 〇> 〇 rH oa m 寸 *-l 03 CN <N CN CN 寸 π σ> in ι〇 • · · · · CO 00 卜 00 co CTi Cf> CTt G\ ε Δ· εε 00 c-< Ci Ό 00 H Ο Η «Η Η <N 寸 VO in r-< 〇 〇) σι VD vo rH rH 〇 〇 〇 〇 —w WQ§ <0 CO w Q Q Q Η H 〇4 Q Q a 6 8 Γ 寸 ε ζ τ OrHOJCO^tlO VOf^CO C^Or-tOJcO^ «HrHrHHHrH rHi-ii-! γΗ〇0Ο4<Ν<ΝΓΜ 附件3(a) 第851 12303 號專利申請案 中文比較數據 民國88年f月呈6 a L 必 winch 96 εΜ τ19 9Π Τ3MM ^ n ^^^^^ fr 丨. Act as her. Members are requested to indicate whether the original substance will be changed after the amendment-ϋ: 0 'g · 00' Δ · 10 !: CN OJ LO VO σ > σ \ \ D0 > Lrn69 ^ 65Δ6 σ »h in co οϊ n (n oj oa οι σ» h cn m cn c \ ri σ \ in co < N r > (N CM 03 < N OrHOJfO inch in vo r- co rH rH Η «Η, rH« —I «Η« —I «Η 〇 > 〇rH oa m inch * -l 03 CN < N CN CN inch π σ > in ι〇 • · · · · CO 00 卜 00 co CTi Cf > CTt G \ ε Δ · εε 00 c- < Ci Ό 00 H Ο Η «Η Η < N inch VO in r- < 〇〇) σι VD vo rH rH 〇〇〇〇—w WQ§ < 0 CO w QQQ Η H 〇4 QQ a 6 8 Γ inch ε ζ τ OrHOJCO ^ tlO VOf ^ CO C ^ Or-tOJcO ^ «HrHrHHHHrH rHi-ii- ! γΗ〇00〇4 < N < ΝΓΜ Annex 3 (a) Patent Application No. 851 12303 Chinese Comparative Data 6 a L 必 w寸 96 εΜ τ19 9Π Τ3ΜΜ ^n^^^^^fr丨 . 担蹈她 £傾請委員明示,本案修正後是否變更原實質内- ϋ:0' g·00' Δ·10!: CN OJ LO VO σ> σ\ \D0> Lrn69^65Δ6 σ» h in co οϊ n (n oj oa οι σ» h卜 cn m cn c\ r-i σ\ in co <N r> (N CM 03 <N OrHOJfO 寸 in vo r- co rH rH Η «Η, rH «—I «Η «—I «Η 〇> 〇 rH oa m 寸 *-l 03 CN <N CN CN 寸 π σ> in ι〇 • · · · · CO 00 卜 00 co CTi Cf> CTt G\ ε Δ· εε 00 c-< Ci Ό 00 H Ο Η «Η Η <N 寸 VO in r-< 〇 〇) σι VD vo rH rH 〇 〇 〇 〇 —w WQ§ <0 CO w Q Q Q Η H 〇4 Q Q a 6 8 Γ 寸 ε ζ τ OrHOJCO^tlO VOf^CO C^Or-tOJcO^ «HrHrHHHrH rHi-ii-! γΗ〇0Ο4<Ν<ΝΓΜ in vo r* co σ\ ο (N CN CN CN OJ Π 寸·ζ 0·ζ9·τ "•ο 6·0 々•86 6·0 in v〇 r- co o £N ON fN (N (N r) 公6 a L 必 winch 96 εΜ τ19 9Π Τ3MM ^ n ^^^^^ fr 丨. Act as her. Members are requested to indicate whether the original substance will be changed after the amendment-ϋ: 0 'g · 00' Δ · 10 !: CN OJ LO VO σ > σ \ \ D0 > Lrn69 ^ 65Δ6 σ »h in co οϊ n (n oj oa οι σ» h cn m cn c \ ri σ \ in co < N r > (N CM 03 < N OrHOJfO inch in vo r- co rH rH Η «Η, rH« —I «Η« —I «Η 〇 > 〇rH oa m inch * -l 03 CN < N CN CN inch π σ > in ι〇 • · · · · CO 00 卜 00 co CTi Cf > CTt G \ ε Δ · εε 00 c- < Ci Ό 00 H Ο Η «Η Η < N inch VO in r- < 〇〇) σι VD vo rH rH 〇〇〇〇—w WQ§ < 0 CO w QQQ Η H 〇4 QQ a 6 8 Γ inch ε ζ τ OrHOJCO ^ tlO VOf ^ CO C ^ Or-tOJcO ^ «HrHrHHHHrH rHi-ii- ! γΗ〇0〇4 < N < ΝΓΜ in vo r * co σ \ ο (N CN CN CN OJ Π inch · ζ 0 · ζ9 · τ " • ο 6 · 0 々 • 86 6 · 0 in v〇r- co o £ N ON fN (N (N r) common A8B8C8D8 六、申請專利範圍 附件1(a): -(锖先閲讀背面之注意事項再填寫本頁) 第85112303號專利申請案 中文申請專利範圍修正本 民國89年)月修正 1.—種用於使丙烯聚合及共聚之觸媒系統,包含有 (a )—種習用吉格列一那塔觸媒成份,基本上由1 . 5 一 6. 0重量%鈦,10-20重置%鎂,40-70重 量%選自包括氯,溴及碘之鹵基;5 - 2 5重量%選自包 括脂族,芳族及脂環族多羧酸之酯類之多羧酸酯;及 0. 1 — 2. 5重量%選自包括磷酸及膦酸之烴酯之有機 磷化合物所組成,其中各烴基具有1個至6個碳原子,該 觸媒成份係藉著具有以下步驟之方法製備: 經濟部智慧財產局貝工消费合作社印製 a) 於溶劑混合物中溶解鎂鹵化物化合物,以形成 均匀溶液,該鎂齒化物選自包括鎂鹵化物與水或醇之鎂鹵 化物錯合物及鎂鹵化物之衍生物,其中鹵原子被烴氧基或 鹵代烴氧基所取代;該溶劑混合物係由有機環氧化合物及 有機磷化合物所組成,以形成均勻溶液,該有機環氧化合 物選自包括脂族烴和二烯之氧化物,鹵化脂族烴及二烴之 氧化物及縮水甘油醚,皆具有2個至8個碳原子,而該有 機磷化合物則選自包括磷酸烷酯,磷酸芳酯,磷酸芳烷酯 ,亞磷酸烷酯,亞磷酸芳酯及亞磷酸芳烷酯,其中烷基具 有1個至4個碳原子,而芳基具有6個至1 0個碳原子: b) 使該均勻溶液與具有通式TiXn(OR) 本紙張尺度適用令國國家標準(CNS)A4規格(210 X 297公釐) 六、申請寻利範圍 之液體欽化合物混合,其中X爲鹵素,R爲相同或相異之 烷基,而η爲〇至4之整數; ·(請先Μ讀背面之注意事項再填寫本頁) c) 添加至少一種輔助沈澱劑,以形成沈澱物,其 選自包括羧酸酐,羧酸,醚及酮; d) 於出現沈澉物之時添加多羧酸酯; e ) 自混合物分離沈澱物,使用鈦化合物 T i Xn( OR) 4_n或其混合物,於情性稀釋劑中處理已 分離之沈澱物,其中X爲鹵素,R爲烴基而可相同或相異 ,且η爲由〇至4之整數;及 f) 使用有機惰性稀釋劑洗滌經處理之沈澱物, (b) —種有機鋁化合物及 (c) 一種具有下式之霄子予體 0¾ R1— Si— R4 I or3 經濟部智慧財產局員工消费合作社印製 其中111爲含有鍵結於矽之一級,二級或三級碳原子之烷 基或環烷基;R2及R3各爲烷基或芳基;而114爲烷基或 環烷基,具有鍵結於矽原子之二級或三級碳原子,尺1及 R 4可相同或相異, 其中Si/Ti莫耳比爲1至400。 2.如申請專利範圍第1項之觸媒系統,其中尺1爲 具有3 - 5個碳原子而具有鏡像對稱性之二級烷基,而 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 2 A8B8C8D8 389772 六、申請專利範圍 R<t爲具有3 - 6個碳原子而具有鏡像對稱性之二級烷基 或環烷基。 3. 如申請專利範圍第2項之觸媒系統,其中尺,及 R 4兩者皆同爲環烷基》 4. 如申請專利範圍第3項之觸媒系統,其中 R 4皆爲環戊基。 5 _如申請專利範圍第1項之觸媒系統,其中尺2及 選自包括甲基,乙基,丙基及丁基。 6. 如申請專利範圍第5項之觸媒系統,其中尺2及 R 3兩者皆同爲甲基。 7. 如申請專利範圍第1項之觸媒系統,其中電子予 體爲環己基甲基二甲氧矽烷,二異丙基二甲氧矽烷,二第 三丁基二甲氧矽烷,環己基異丙基二甲氧矽烷或二環戊基 二甲氧矽烷。 8. 如申請專利範圍第7項之觸媒系統,其中該電子 予體爲二環戊基二甲氧矽烷。 9. 如申請專利範圍第1項之觸媒系統,其中該有機 鋁化合物爲通式A 1 R 之烷基鋁,其中R >爲具有1 一 8個碳原子之烷基或鹵素,R /與至少一個R1相同或 相異而爲烷基,且R /相同或相異。 1 〇 .如申請專利範圍第9項之觸媒系統,其中該有· 機鋁化合物係選自包括三烷基鋁,烷基鋁二鹵化物,三烷 氧基鋁及二烷基鋁鹵化物。 1 1 .如申請專利範圍第1 0項之觸媒系統,其中該 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) *- 訂---------線! .(請先《讀背面之注意事項再填寫本頁) 、 經濟部智慧財產局具工消费合作社印製 * 3 - A8B8C8D8 389772 力、申請專利範圍 有機鋁化合物爲三烷基鋁。 1 2 .如申請專利範圍第1 1項之觸媒系統,其中該 有機鋁化合物爲三乙基鋁或三異丁基鋁》 1 3 .如申請專利範圍第1項之觸媒系統,其中a 1 /Si莫耳比爲〇. 5至500。 1 4 種使丙烯聚合之方法,其包括: (a) 選擇習用吉格列-那塔觸媒成份,基本上由 1. 5—6. 0重量%鈦,10-20重量%鎂,40- 7 0重量%選自包括氯,溴及碘之鹵基;5 — 2 5重量% 選自包括脂族,芳族及脂環族多羧酸之酯類之多羧酸酯; 及0· 1 — 2. 5重量%選自包括磷酸及膦酸之烴酯之有 機磷化合物所組成,其中各烴基具有1個至6個碳原子, 該觸媒成份係藉著具有以下步驟之方法製備: a ) 於溶劑混合物中溶解鎂鹵化物化合物,以形成 均勻溶液,該鎂齒化物選自包括鎂鹵化物與水或醇之鎂鹵 化物錯合物及鎂菌化物之衍生物,其中鹵原子被烴氧基或 鹵代烴氧基所取代;該溶劑混合物係由有機環氧化合物及 有機磷化合物所組成,以形成均勻溶液,該有機環氧化合 物選自包括脂族烴和二烯之氧化物,鹵化脂族烴及二烴之 氧化物及縮水甘油醚,皆具有2個至8個碳原子,而該有 機磷化合物則選自包括磷酸烷酯,磷酸芳酯,磷酸芳烷酯 ,亞磷酸烷酯,亞磷酸芳酯及亞磷酸芳烷酯,其中烷基具 有1個至4個碳原子,而芳基具有6個至1 0個碳原子; b ) 使該均勻溶液與具有通式TiXnCOR)^!-^ 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公« ) 一 - 訂------I--線! ·(請先閱讀背面之注意事項再填寫本頁) ,0. 經濟部智慧財產局貝工消费合作社印製 -4 - A8B8C8D8 38977S 六、申請專利範圍 之液體鈦化合物混合,其中X爲齒^素,R爲相同或相異之 烷基,而η爲〇至4之整數; ί猜先»讀背面之注意事項再填寫本頁) c ) 添加至少一種輔助沈澱劑,以形成沈澱物,其 選自包括羧酸酐,羧酸,醚及酮; d) 於出現沈澱物之時添加多羧酸酯; e) 自混合物分離沈澱物,使用鈦化合物 T i X n ( 0 R ) 4_n或其混合物,於惰性稀釋劑中處理已 分離之沈澱物,其中X爲鹵素,R爲烴基而可相同或相異 ,且η爲由〇至4之整數;及 f) 使用有機惰性稀釋劑洗滌經處理之沈澱物, (b) 使該觸媒與有機鋁化合物接觸; (c) 於步驟(b)之同時或之後,使該觸媒與電子予 體接觸, 該電子予體具有如下通式: 0R2 R·) — Si — R4 I 〇R3 經濟部智慧財產局員工消费合作社印髮 其中Rl爲含有一級,二級或三級碳原子之烷基或環烷基 ;R2及R 3爲烷基或芳基;而R4爲烷基或環烷基’具有 鍵結於矽原子之二級或三級碳鼠子’ R ^及R 4相同或相異 » 其中S i/Ti莫比爲1至400, 本紙張尺度適用中國國家標準(CNS)A4規格(210 * 297公釐) 5 A8B8C8D8 六、申請寻利範圍 (d) 將該觸媒導入含有該單體之聚合反應區內。 <請先闥讀背面之注意事項再填寫本頁) 1 5 _如申請專利範圍第1 4項之方法,其中只1爲 具有3 - 5個碳原子而具有鏡像對稱性之二級烷基,而 R 4爲具有3 _ 6個碳原子而具有鏡像對稱性之二級院基 或環烷基。 1 6 .如申請專利範圍第1 5項之方法,其中Rl& R 4兩者皆同爲環烷基》 1 7 ·如申請專利範圍第1 6項之方法,其中Rl& R 4兩者皆爲環戊基。 .1 8 :如申請專利範圍第1 7項之方法,其中電子予 體爲環己基甲基二甲氧砂院,二異丙基二甲氧较院,二第 三丁基二甲氧矽烷,環己基異丙基二甲氧矽烷或二環戊基 二甲氧矽烷。 1 9 ·如申請專利範圍第1 8項之方法,其中該電子 予體爲二環戊基二甲氧矽烷。 _經濟部智慧財產局員工消费合作社印製 2 0 .如申請專利範圍第1 4項之方法,其中該有機 鋁化合物爲通式A 1R < 3之烷基鋁,其中R -爲具有1 —8個碳原子之焼基或鹵索,R /與至少一個R1相同或 相異而爲烷基,且R >相同或相異。 2 1 _如申請專利範圍第2 0項之方法,其中該有機 鋁化合物係選自包括三烷基鋁,烷基鋁二鹵化物,三院氧 基鋁及二烷基鋁鹵化物。 2 2 .如申請專利範圍第2 1項之方法,其中該有機 鋁化合物爲三烷基鋁。 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公爱〉 389772 A8 B8 C8 D8 六、申請專利範圍 2. 3.如申請專利範圍第2 2項之方法,其中該有機 鋁化合物爲三乙基鋁。 2 4 .如申請專利範園第1 4項之方法,其中該單體 爲丙烯。 2 5 ·如申請專利範圍第1 4項之方法,其中於步驟 (c)之後有其他步驟,包括: 藉著使少置單體與該觸媒接觸,而使該觸媒預聚。 26.如申請專利範困第14項之方法,其中該反應 區含有額外置之該有機鋁化合物及該電子予體。 2 7 :如申請專利範圔第1 4項之方法,其中該方法 之特徵爲製造一種聚合物產物,其二甲苯可溶物部分介於 聚合物產物之0. 6 — 3. Owt%範國內· 28. 如申請專利範圍第14項之方法,其另外包括 添加第二種單體,以形成共聚物· 29. 如申請專利範圍第14項之方法,其中A1/ Si莫耳比爲0. 5至500。 <請先鬮讀背面之注意事項再填寫本頁) d T --線· 經濟部智慧財產局貝工消费合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公爱)A8B8C8D8 VI. Annex 1 (a) of the scope of patent application:-(锖 Please read the notes on the back before filling this page) No. 85112303 Patent Application Chinese Application for Patent Scope Amendment The Republic of China 89) Month Amendment The catalyst system for polymerizing and copolymerizing propylene contains (a) —a conventional Giglia-Nata catalyst component, which is basically composed of 1.5 to 6.0 weight percent titanium, and 10 to 20% reset magnesium. 40-70% by weight is selected from halogen groups including chlorine, bromine and iodine; 5-25% by weight is selected from polycarboxylic acid esters including aliphatic, aromatic and cycloaliphatic polycarboxylic acids; and 0. 1-2.5% by weight of organic phosphorus compounds selected from the group consisting of hydrocarbon esters of phosphoric acid and phosphonic acid, wherein each hydrocarbon group has 1 to 6 carbon atoms, and the catalyst component is prepared by a method having the following steps: Printed by Shelley Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs a) Dissolving a magnesium halide compound in a solvent mixture to form a homogeneous solution, the magnesium dentate is selected from a magnesium halide complex including magnesium halide and water or alcohol and Derivatives of magnesium halides in which the halogen atom is replaced by an alkoxy or halogenated hydrocarbon The solvent mixture is composed of an organic epoxy compound and an organic phosphorus compound to form a homogeneous solution. The organic epoxy compound is selected from the group consisting of oxides of aliphatic hydrocarbons and diene, halogenated aliphatic hydrocarbons, and dihydrocarbons. The oxides and glycidyl ethers have 2 to 8 carbon atoms, and the organic phosphorus compound is selected from the group consisting of alkyl phosphates, aryl phosphates, aralkyl phosphates, alkyl phosphites, aryl phosphites and Aralkyl phosphite, in which the alkyl group has 1 to 4 carbon atoms and the aryl group has 6 to 10 carbon atoms: b) the homogeneous solution and the general formula TiXn (OR) National Standard (CNS) A4 Specification (210 X 297 mm) 6. Mixing of liquid cyanide compounds applying for profit, where X is halogen, R is the same or different alkyl group, and η is an integer from 0 to 4. ; (Please read the notes on the back before filling this page) c) Add at least one auxiliary precipitant to form a precipitate, which is selected from the group consisting of carboxylic anhydride, carboxylic acid, ether and ketone; Adding polycarboxylic acid esters at the time of the material; e) from the mixture To separate the precipitate, use the titanium compound T i Xn (OR) 4_n or a mixture thereof to treat the separated precipitate in an emotional diluent, where X is a halogen, R is a hydrocarbon group and may be the same or different, and η is given by An integer of 0 to 4; and f) washing the treated precipitate with an organic inert diluent, (b) an organoaluminum compound and (c) a seedling precursor having the formula 0¾ R1—Si—R4 I or3 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, where 111 is an alkyl or cycloalkyl group containing one, two or three carbon atoms bonded to silicon; R2 and R3 are each alkyl or aryl; and 114 is Alkyl or cycloalkyl, having secondary or tertiary carbon atoms bonded to a silicon atom, Chi 1 and R 4 may be the same or different, wherein the Si / Ti molar ratio is 1 to 400. 2. As for the catalyst system of the first item in the scope of patent application, where ruler 1 is a secondary alkyl group with 3 to 5 carbon atoms and mirror symmetry, and this paper size applies the Chinese National Standard (CNS) A4 specification ( 210 X 297 mm) 2 A8B8C8D8 389772 6. The scope of patent application R < t is a secondary alkyl or cycloalkyl group with 3 to 6 carbon atoms and mirror symmetry. 3. If the catalyst system in the scope of patent application No. 2 in which both the ruler and R 4 are both cycloalkyl "4. If the catalyst system in the scope of patent application No. 3 in which R 4 is cyclopentyl base. 5 _ The catalyst system according to item 1 of the scope of patent application, wherein the ruler 2 and is selected from the group consisting of methyl, ethyl, propyl and butyl. 6. For example, the catalyst system of item 5 of the patent scope, in which both the ruler 2 and R 3 are methyl. 7. For example, the catalyst system of the scope of patent application, wherein the electron donor is cyclohexylmethyldimethoxysilane, diisopropyldimethoxysilane, di-tert-butyldimethoxysilane, cyclohexyl iso Propyldimethoxysilane or dicyclopentyldimethoxysilane. 8. If the catalyst system according to item 7 of the patent application scope, wherein the electron donor is dicyclopentyldimethoxysilane. 9. The catalyst system according to item 1 of the scope of patent application, wherein the organoaluminum compound is an alkyl aluminum of the general formula A 1 R, where R > is an alkyl or halogen having 1 to 8 carbon atoms, R / It is the same or different from at least one R1 and is an alkyl group, and R / is the same or different. 10. The catalyst system according to item 9 of the scope of the patent application, wherein the organic aluminum compound is selected from the group consisting of trialkylaluminum, alkylaluminum dihalide, trialkoxyaluminum, and dialkylaluminum halide. . 1 1. If the catalyst system of item 10 in the scope of patent application, the paper size is applicable to the Chinese National Standard (CNS) A4 specification (210 X 297 mm) *-Order --------- line !! (Please read the "Notes on the back side before filling out this page"), printed by the Industrial Property Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs * 3-A8B8C8D8 389772, the scope of patent application The organoaluminum compound is trialkylaluminum. 1 2. The catalyst system according to item 11 of the scope of patent application, wherein the organoaluminum compound is triethylaluminum or triisobutyl aluminum. 1 3. The catalyst system according to item 1 of the scope of patent application, where a 1 / Si molar ratio is 0.5 to 500. 14 methods for polymerizing propylene, including: (a) selecting conventional Giglia-Nata catalyst components, consisting essentially of 1.5-6. 0 wt% titanium, 10-20 wt% magnesium, 40- 70% by weight is selected from halogen groups including chlorine, bromine and iodine; 5-2 55% by weight is selected from polycarboxylic acid esters including aliphatic, aromatic and cycloaliphatic polycarboxylic acids; and 0.1 — 2.5% by weight of organic phosphorus compounds selected from the group consisting of hydrocarbon esters of phosphoric acid and phosphonic acid, wherein each hydrocarbon group has 1 to 6 carbon atoms, and the catalyst component is prepared by a method having the following steps: a ) Dissolving a magnesium halide compound in a solvent mixture to form a homogeneous solution, the magnesium dentate is selected from the group consisting of a magnesium halide complex of magnesium halide with water or an alcohol, and a derivative of a magnesium mycide, wherein the halogen atom is replaced by a hydrocarbon Alkoxy or halogenated alkoxy; the solvent mixture is composed of an organic epoxy compound and an organic phosphorus compound to form a homogeneous solution, the organic epoxy compound is selected from oxides including aliphatic hydrocarbons and diene, Oxides and glycidyl ethers of halogenated aliphatic and dihydrocarbons, each with 2 8 carbon atoms, and the organophosphorus compound is selected from the group consisting of alkyl phosphates, aryl phosphates, aralkyl phosphates, alkyl phosphites, aryl phosphites, and aralkyl phosphites, wherein the alkyl group has 1 to 4 carbon atoms, and the aryl group has 6 to 10 carbon atoms; b) the homogeneous solution and the general formula TiXnCOR) ^!-^ This paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 Public «) I-order ------ I-- line! · (Please read the precautions on the back before filling this page), 0. Printed by the Shelley Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs-4-A8B8C8D8 38977S VI. Patented liquid titanium compound mixture, where X is tooth element , R is the same or different alkyl group, and η is an integer from 0 to 4; Guess first »Read the notes on the back and then fill out this page) c) Add at least one auxiliary precipitant to form a precipitate. Including carboxylic anhydrides, carboxylic acids, ethers and ketones; d) adding polycarboxylic acid esters when a precipitate appears; e) separating the precipitate from the mixture using a titanium compound T i X n (0 R) 4_n or a mixture thereof, Treating the separated precipitate in an inert diluent, where X is halogen, R is a hydrocarbon group and may be the same or different, and η is an integer from 0 to 4; and f) the treated precipitate is washed with an organic inert diluent (B) contacting the catalyst with an organoaluminum compound; (c) simultaneously or after step (b), contacting the catalyst with an electron donor, the electron donor having the general formula: 0R2 R · ) — Si — R4 I 〇R3 Intellectual Property of the Ministry of Economic Affairs Bureau Consumer Consumption Cooperatives issued R1 is an alkyl or cycloalkyl group containing primary, secondary, or tertiary carbon atoms; R2 and R3 are alkyl or aryl groups; and R4 is an alkyl or cycloalkyl group with a bond The secondary or tertiary carbon rat 'R ^ and R 4 are the same as or different from each other due to the silicon atom »Among them, the Mo / Ti ratio is 1 to 400. The paper size is applicable to China National Standard (CNS) A4 (210 * 297 mm) 5 A8B8C8D8 6. Application for profit-seeking scope (d) The catalyst is introduced into the polymerization reaction zone containing the monomer. < Please read the notes on the back before filling in this page) 1 5 _If the method of patent application No. 14 is used, only 1 is a secondary alkyl group with 3 to 5 carbon atoms and mirror symmetry R 4 is a secondary or cycloalkyl group having 3 to 6 carbon atoms and mirror symmetry. 16. The method according to item 15 of the patent application, wherein both Rl & R 4 are the same as the cycloalkyl group. 1 7 · The method according to item 16 of the patent application, wherein both Rl & R 4 are Is cyclopentyl. .18: The method according to item 17 of the scope of patent application, wherein the electron donor is a cyclohexylmethyldimethoxyacetate compound, a diisopropyldimethoxy compound compound, a second and third butyldimethoxysilane, Cyclohexyl isopropyl dimethoxysilane or dicyclopentyl dimethoxysilane. 19 · The method of claim 18 in the scope of patent application, wherein the electron donor is dicyclopentyldimethoxysilane. _ Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 20. For example, the method of claim 14 in the scope of patent application, wherein the organoaluminum compound is an aluminum alkyl of the general formula A 1R < 3, where R-is 1- A fluorenyl or halide group of 8 carbon atoms, R / is the same or different from at least one R1 and is an alkyl group, and R > is the same or different. 2 1 _ The method of claim 20, wherein the organoaluminum compound is selected from the group consisting of trialkylaluminum, alkylaluminum dihalides, triplex oxyaluminums and dialkylaluminum halides. 2 2. The method according to item 21 of the patent application scope, wherein the organoaluminum compound is a trialkylaluminum. This paper size is applicable to Chinese National Standard (CNS) A4 specifications (210 X 297 Public Love) 389772 A8 B8 C8 D8 VI. Application for patent scope 2. 3. If the method of item 22 of patent scope is applied, where the organoaluminum compound is Triethylaluminum 2 4. The method according to item 14 of the patent application park, wherein the monomer is propylene. 2 5 · The method according to item 14 of the patent application scope, wherein there are other steps after step (c) The steps include: pre-polymerizing the catalyst by contacting a few monomers with the catalyst. 26. The method according to item 14 of the patent application, wherein the reaction zone contains the organic aluminum compound additionally disposed 6-Such as the method of claim 14 of the patent application, wherein the method is characterized by the manufacture of a polymer product, the xylene soluble part of the polymer product is 0.6- 3. Owt% Fan Domestic · 28. If the method of applying for the scope of the patent No. 14 further includes adding a second monomer to form a copolymer · 29. If the method of applying for the scope of the patent No. 14 in which A1 / Si Morse ratio is 0.5 to 500. < Please read the notes on the back first (Fill in this page) d T-Printed by Shelley Consumer Cooperative, Bureau of Intellectual Property, Ministry of Economic Affairs This paper is sized for China National Standard (CNS) A4 (210 X 297 public love)
TW85112303A 1996-10-08 1996-10-08 A catalyst system to produce highly crystalline polypropylene TW389772B (en)

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