RU2008114518A - Катализаторы полимеризации и способ получения полимеров с бимодальным молекулярно-массовым распределением в одном реакторе - Google Patents
Катализаторы полимеризации и способ получения полимеров с бимодальным молекулярно-массовым распределением в одном реакторе Download PDFInfo
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Abstract
1. Каталитическая композиция, содержащая первое металлоценовое соединение, второе металлоценовое соединение, активатор-носитель и алюминийорганическое соединение, где: ! (а) первое металлоценовое соединение имеет формулу ! (Х1)(Х2R1 2)(X3)(X4)M1; ! где (Х1) означает циклопентадиенил, инденил или флуоренил; ! где (Х2) означает флуоренил; ! где (Х1) и (Х2) связаны дизамещенной мостиковой группой, один атом которой связан и с (Х1), и с (Х2), и где атом представляет собой углерод или кремний; ! где первым заместителем дизамещенной мостиковой группы является алифатическая или ароматическая группа, в которой имеется от 1 до, примерно, 10 атомов углерода; ! где вторым заместителем дизамещенной мостиковой группы является насыщенная или ненасыщенная алифатическая группа, в которой имеется от 3 до, примерно, 10 атомов углерода; ! где R1 является Н или алкильной группой, в которой имеется от 1 до, примерно, 4 атомов углерода; ! где (X3) и (X4) независимо друг от друга являются галогеном; ! где М1 означает Zr или Hf; ! (б) второе металлоценовое соединение имеет формулу ! ! где R2 означает Н или -СН3; ! где R3 означает СН2=СНСН2-, СН2=СН(СН2)2-, Ph(CH2)3-, СН3(СН2)3- или Н; ! где Х5 и Х6 независимо друг от друга являются галогенами; ! где M2 означает Zr или Hf. ! 2. Каталитическая композиция по п.1, в которой отношение первого металлоценового соединения ко второму металлоценовому соединению составляет от, примерно, 1:10 до, примерно, 10:1. ! 3. Каталитическая композиция по п.1, в которой отношение первого металлоценового соединения ко второму металлоценовому соединению составляет от, примерно, 1:5 до, примерно, 5:1. ! 4. Каталитическая композиция по п.1, в которой отношение первого металлоценового соедине
Claims (29)
1. Каталитическая композиция, содержащая первое металлоценовое соединение, второе металлоценовое соединение, активатор-носитель и алюминийорганическое соединение, где:
(а) первое металлоценовое соединение имеет формулу
(Х1)(Х2R1 2)(X3)(X4)M1;
где (Х1) означает циклопентадиенил, инденил или флуоренил;
где (Х2) означает флуоренил;
где (Х1) и (Х2) связаны дизамещенной мостиковой группой, один атом которой связан и с (Х1), и с (Х2), и где атом представляет собой углерод или кремний;
где первым заместителем дизамещенной мостиковой группы является алифатическая или ароматическая группа, в которой имеется от 1 до, примерно, 10 атомов углерода;
где вторым заместителем дизамещенной мостиковой группы является насыщенная или ненасыщенная алифатическая группа, в которой имеется от 3 до, примерно, 10 атомов углерода;
где R1 является Н или алкильной группой, в которой имеется от 1 до, примерно, 4 атомов углерода;
где (X3) и (X4) независимо друг от друга являются галогеном;
где М1 означает Zr или Hf;
(б) второе металлоценовое соединение имеет формулу
где R2 означает Н или -СН3;
где R3 означает СН2=СНСН2-, СН2=СН(СН2)2-, Ph(CH2)3-, СН3(СН2)3- или Н;
где Х5 и Х6 независимо друг от друга являются галогенами;
где M2 означает Zr или Hf.
2. Каталитическая композиция по п.1, в которой отношение первого металлоценового соединения ко второму металлоценовому соединению составляет от, примерно, 1:10 до, примерно, 10:1.
3. Каталитическая композиция по п.1, в которой отношение первого металлоценового соединения ко второму металлоценовому соединению составляет от, примерно, 1:5 до, примерно, 5:1.
4. Каталитическая композиция по п.1, в которой отношение первого металлоценового соединения ко второму металлоценовому соединению составляет от, примерно, 1:2 до, примерно, 2:1.
5. Каталитическая композиция по п.1, в которой первый заместитель дизамещенной мостиковой группы представляет собой фенил или метил.
6. Каталитическая композиция по п.1, в которой второй заместитель дизамещенной мостиковой группы представляет собой бутенил, пентенил или гексенил.
9. Каталитическая композиция по п.1, в которой активатор-носитель представляет собой фторированный оксид алюминия, хлорированный оксид алюминия, бромированный оксид алюминия, сульфатированный оксид алюминия, фторированный диоксид кремния-оксид алюминия, хлорированный диоксид кремния-оксид алюминия, бромированный диоксид кремния-оксид алюминия, сульфатированный диоксид кремния-оксид алюминия, фторированный диоксид кремния-диоксид циркония, хлорированный диоксид кремния-диоксид циркония, бромированный диоксид кремния-диоксид циркония, сульфатированный диоксид кремния-диоксид циркония или любое их сочетание.
10. Каталитическая композиция по п.1, в которой активатор-носитель содержит твердый оксид, обработанный электроноакцепторным анионом,
где твердый оксид представляет собой диоксид кремния, оксид алюминия, диоксид кремния-оксид алюминия, фосфат алюминия, гетерополивольфраматы, оксид титана, оксид циркония, оксид магния, оксид бора, оксид цинка, любые смешанные оксиды или любые их сочетания;
электроноакцепторным анионом является фторид, хлорид, бромид, фосфат, трифлат, бисульфат, сульфат или любое их сочетание.
11. Каталитическая композиция по п.1, в которой активатор-носитель дополнительно содержит металл или ион металла, где металл или ион металла представляет собой цинк, никель, ванадий, серебро, медь, галлий, олово, вольфрам, молибден или любое их сочетание.
12. Каталитическая композиция по п.11, в которой активатор-носитель представляет собой обогащенный цинком хлорированный оксид алюминия, обогащенный цинком фторированный оксид алюминия, обогащенный цинком хлорированный диоксид кремния-оксид алюминия, обогащенный цинком фторированный диоксид кремния-оксид алюминия, обогащенный цинком сульфатированный оксид алюминия или любое их сочетание.
13. Каталитическая композиция по п.1, в которой активатор-носитель содержит сшитую глину.
14. Каталитическая композиция по п.13, в которой сшитая глина содержит диоксид кремния, диоксид кремния-оксид алюминия или их сочетание.
15. Каталитическая композиция по п.13, в которой сшитая глина содержит аллофан, смектит, галлуазит, глины со смешанными слоями, волокнистые глины, серпентиновую глину, вермикулит, слюду, фторслюду, хлорит, иллит, лапонит, сапонит или любые их сочетания.
16. Каталитическая композиция по п.1, в которой алюминийорганическое соединение имеет формулу
(R2)3Al;
где (R2) означает этильную группу, пропильную группу, бутильную группу, гексильную группу или изобутильную группу.
17. Каталитическая композиция по п.1, в которой алюминийорганическое соединение имеет формулу
Al(X9)n(X10)3-n,
где (X9) означает углеводород, содержащий от 1 до, примерно, 20 атомов углерода, (X10) означает алкоксид или арилоксид, содержащий от 1 до, примерно, 20 атомов углерода, галоген или гидрид, n является числом от 1 до 3, включительно.
18. Каталитическая композиция по п.1, в которой алюминийорганическое соединение представляет собой триметилалюминий, триэтилалюминий, три-н-пропилалюминий, этоксид диэтилалюминия, три-н-бутилалюминий, гидрид диизобутилалюминия, триизобутилалюминий, хлорид диэтилалюминия или любое их сочетание.
19. Каталитическая композиция по п.1, в которой весовое отношение алюминийорганического соединения к активатору-носителю составляет от, примерно, 10:1 до, примерно, 1:1000.
20. Каталитическая композиция по п.1, дополнительно содержащая, по меньшей мере, один алюмоксан, по меньшей мере, одно цинкорганическое соединение, по меньшей мере, одно борорганическое соединение, по меньшей мере, одно ионизирующее ионное соединение или любое их сочетание.
21. Способ полимеризации олефинов в присутствии каталитической композиции по п.1, включающий приведение в контакт каталитической композиции, по меньшей мере, с одним типом олефиновых мономеров в условиях реакции с получением полимера.
22. Способ по п.21, в котором условия реакции включают температуру полимеризации от, примерно, 60°С до, примерно, 280°С.
23. Способ по п.21, в котором каталитическую композицию и, по меньшей мере, один тип олефиновых мономеров вводят в контакт в газофазном реакторе, петлевом реакторе, корпусном реакторе с мешалкой или любом их сочетании.
24. Способ получения каталитическую композицию по п.1, включающий введение в контакт первого металлоценового соединения, второго металлоценового соединения, активатора-носителя и алюминийорганического соединения.
26. Способ получения моноциклопентадиенильного соединения формулы 2(1,3R2R4Cp)MCl3 или его изомеров, включающий флегмирование в течение, примерно, 20 часов растворителя, содержащего
(а) соединение тетрахлорида металла;
(б) соединение формулы (1,3R2R4Cp)2MCl2;
и обеспечивающий выход моноциклопентадиенильного соединения, по меньшей мере, около 70%;
где M означает Zr или Hf;
R2 означает Н, алкильную группу или алкенильную группу;
R4 означает Н, алкильную группу или алкенильную группу.
27. Способ по п.26, в котором R2 является алкильной группой, и R4 является Н или алкильной группой.
28. Способ по п.26, дополнительно включающий выделение моноциклопентадиенильного соединения в виде твердого материала.
29. Способ по п.28, в котором выделение соединения в виде твердого материала включает введение реакционной смеси в контакт с СН2Сl2 и пентаном, гексаном, гептаном или любым их сочетанием.
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SG176790A1 (en) | 2009-06-16 | 2012-01-30 | Chevron Phillips Chemical Co | Oligomerization of alpha olefins using metallocene-ssa catalyst systems and use of the resultant polyalphaolefins to prepare lubricant blends |
MX2012000254A (es) | 2009-06-29 | 2012-01-25 | Chevron Philips Chemical Company Lp | El uso de catalizadores de depuracion de hidrogeno para controlar niveles de hidrogeno y peso molecular de polimero en un reactor de polimerizacion. |
BRPI1014662B1 (pt) | 2009-06-29 | 2021-06-29 | Chevron Phillips Chemical Company Lp | Processo de polimerização de olefina |
US20110082323A1 (en) | 2009-10-06 | 2011-04-07 | Chevron Phillips Chemical Company Lp | Oligomerization of olefin waxes using metallocene-based catalyst systems |
US8383754B2 (en) | 2010-04-19 | 2013-02-26 | Chevron Phillips Chemical Company Lp | Catalyst compositions for producing high Mz/Mw polyolefins |
US8288487B2 (en) | 2010-07-06 | 2012-10-16 | Chevron Phillips Chemical Company Lp | Catalysts for producing broad molecular weight distribution polyolefins in the absence of added hydrogen |
US8309747B2 (en) | 2010-07-06 | 2012-11-13 | Chevron Phillips Chemical Company Lp | Process for synthesizing bridged cyclopentadienyl-indenyl metallocenes |
US8629292B2 (en) | 2010-10-07 | 2014-01-14 | Chevron Phillips Chemical Company Lp | Stereoselective synthesis of bridged metallocene complexes |
US8637616B2 (en) | 2010-10-07 | 2014-01-28 | Chevron Philips Chemical Company Lp | Bridged metallocene catalyst systems with switchable hydrogen and comonomer effects |
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