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RU97101172A - CATALYTIC POLYMERIZATION SYSTEMS, THEIR PRODUCTION AND APPLICATION - Google Patents

CATALYTIC POLYMERIZATION SYSTEMS, THEIR PRODUCTION AND APPLICATION

Info

Publication number
RU97101172A
RU97101172A RU97101172/04A RU97101172A RU97101172A RU 97101172 A RU97101172 A RU 97101172A RU 97101172/04 A RU97101172/04 A RU 97101172/04A RU 97101172 A RU97101172 A RU 97101172A RU 97101172 A RU97101172 A RU 97101172A
Authority
RU
Russia
Prior art keywords
volume
solution
total pore
catalyst system
pore volume
Prior art date
Application number
RU97101172/04A
Other languages
Russian (ru)
Other versions
RU2167883C2 (en
Inventor
Аллен Вогн Джордж
Николас Спека Энтони
Брант Патрик
Энн Мари Канич Джо
Original Assignee
Эксон Кемикэл Пейтентс Инк.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Эксон Кемикэл Пейтентс Инк. filed Critical Эксон Кемикэл Пейтентс Инк.
Publication of RU97101172A publication Critical patent/RU97101172A/en
Application granted granted Critical
Publication of RU2167883C2 publication Critical patent/RU2167883C2/en

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Claims (12)

1. Способ приготовления каталитической системы на носителе, включающий (а) введение пористого носителя в контакт с раствором, включающим металлоценовый каталитический компонент и активатор, где общий объем раствора находится в интервале значений от объема, менее чем в три раза превышающего общий объем пор пористого носителя, до объема, превышающего однократный общий объем пор пористого носителя; и (б) сушку образовавшейся каталитической системы.1. A method of preparing a supported catalyst system comprising (a) bringing the porous support into contact with a solution comprising a metallocene catalyst component and an activator, wherein the total solution volume is in the range of a volume less than three times the total pore volume of the porous carrier up to a volume exceeding a single total pore volume of the porous support; and (b) drying the resulting catalyst system. 2. Способ приготовления каталитической системы на носителе, включающий (а) введение пористого носителя в контакт с раствором, включающим металлоценовый каталитический компонент и активатор, где общий объем раствора находится в интервале значений от объема, меньшего того объема, при котором образуется взвесь, до объема, превышающего однократный общий объем пор пористого носителя; и (б) сушку образовавшейся каталитической системы. 2. A method of preparing a supported catalyst system, comprising (a) bringing the porous support into contact with a solution comprising a metallocene catalyst component and an activator, wherein the total volume of the solution is in the range from a volume less than the volume at which the suspension forms to the volume exceeding a single total pore volume of the porous support; and (b) drying the resulting catalyst system. 3. Способ приготовления каталитической системы на носителе, включающий введение пористого носителя в контакт с двумя или большим числом растворов, один из которых включает металлоценовый каталитический компонент, а другой включает активатор, где совместный объем растворов находится в интервале значений от объема, меньшего того объема, при котором образуется взвесь, до объема, превышающего однократный общий объем пор пористого носителя. 3. A method of preparing a supported catalyst system comprising contacting a porous support with two or more solutions, one of which includes a metallocene catalyst component, and the other includes an activator, where the joint volume of the solutions is in the range of values from a volume less than that in which a suspension is formed, to a volume exceeding a single total pore volume of the porous support. 4. Способ по п. 1 или 2, где общий объем раствора(ов) находится в интервале значений от объема, меньшего того объема, при котором образуется взвесь, до объема, превышающего однократный общий объем пор пористого носителя. 4. The method according to p. 1 or 2, where the total volume of the solution (s) is in the range of values from a volume less than the volume at which a suspension is formed to a volume exceeding a single total pore volume of the porous support. 5. Способ по любому из предыдущих пунктов, где общий объем раствора (ов) составляет от 2,5-кратного общего объема пор пористого носителя до 1,05-кратного общего объема пор пористого носителя. 5. The method according to any one of the preceding paragraphs, where the total volume of the solution (s) is from 2.5 times the total pore volume of the porous carrier to 1.05 times the total pore volume of the porous carrier. 6. Способ по любому из предыдущих пунктов, где общий объем раствора(ов) составляет от 2,4-кратного общего объема пор пористого носителя до 1,4-кратного общего объема пор пористого носителя. 6. The method according to any one of the preceding paragraphs, where the total volume of the solution (s) is from 2.4 times the total pore volume of the porous carrier to 1.4 times the total pore volume of the porous carrier. 7. Способ по любому из предыдущих пунктов, где раствор (ы) включает (ют) два или большее число металлоценовых каталитических компонентов и/или два или большее число активаторов. 7. The method according to any one of the preceding paragraphs, where the solution (s) comprises (s) two or more metallocene catalyst components and / or two or more activators. 8. Способ по любому из предыдущих пунктов, где перед введением в контакт с раствором (ами) пористый носитель обезвоживают. 8. The method according to any one of the preceding paragraphs, where the porous carrier is dehydrated before being brought into contact with the solution (s). 9. Способ по любому из предыдущих пунктов, где молярное соотношение между металлом активатора и переходным металлом металлоценового каталитического компонента составляет от 20:1 до 800:1. 9. The method according to any one of the preceding paragraphs, where the molar ratio between the activator metal and the transition metal of the metallocene catalyst component is from 20: 1 to 800: 1. 10. Способ полимеризации олефинов индивидуально или в сочетании с одним или несколькими другими олефиновыми мономерами, включающий полимеризацию в присутствии каталитической системы на носителе, приготовленной способом по любому из предыдущих пунктов. 10. A method for polymerizing olefins individually or in combination with one or more other olefin monomers, comprising polymerizing in the presence of a supported catalyst system prepared by the method of any one of the preceding paragraphs. 11. Каталитическая система на носителе, полученная способом по любому из пп. 1-9. 11. The supported catalyst system obtained by the method according to any one of claims. 1-9. 12. Способ по п. 1, где раствор включает диметилсилил(тетраметилциклопентадиенил)(адамантиламидо)титандихлорид. 12. The method according to p. 1, where the solution includes dimethylsilyl (tetramethylcyclopentadienyl) (adamantylamido) titanedichloride.
RU97101172/04A 1994-06-24 1995-06-21 Catalytic polymerization systems, preparation and application thereof RU2167883C2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US26553394A 1994-06-24 1994-06-24
US08/265.533 1994-06-24
US41281095A 1995-03-29 1995-03-29
US08/412.810 1995-03-29

Publications (2)

Publication Number Publication Date
RU97101172A true RU97101172A (en) 1999-02-20
RU2167883C2 RU2167883C2 (en) 2001-05-27

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Country Status (12)

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US (1) US5863853A (en)
EP (1) EP0766702B1 (en)
JP (1) JP3699479B2 (en)
KR (1) KR100376405B1 (en)
CN (1) CN1119355C (en)
AT (1) ATE207085T1 (en)
AU (1) AU686836B2 (en)
CA (1) CA2193410C (en)
DE (1) DE69523308T2 (en)
ES (1) ES2165425T3 (en)
RU (1) RU2167883C2 (en)
WO (1) WO1996000245A1 (en)

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