Catalyst system for polymerization of an olefin

US2016311950A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016311950-A1
Application numberUS-201415106061-A
CountryUS
Kind codeA1
Filing dateDec 19, 2014
Priority dateDec 20, 2013
Publication dateOct 27, 2016
Grant date

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Abstract

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A process for the preparation of a catalyst system for olefin polymerization, including: A) providing said procatalyst obtainable via a process comprising: i) contacting a compound R 4 z MgX 4 2-z with an alkoxy- or aryloxy-containing silane compound to give a first intermediate reaction product, ii) optionally contacting the solid product obtained in step i) with at least one activating compound selected from an activating electron donor or metal alkoxide compound; iii) contacting the first or second intermediate reaction product, with a halogen-containing Ti-compound and optionally an internal electron donor to obtain the procatalyst; and B) contacting the procatalyst with a co-catalyst and at least diethylaminotriethoxysilane as the external donor. Further disclosed is a catalyst system obtained by the process; a process for preparing a polyolefin by contacting at least one olefin with the catalyst system; a polyolefin obtained thereby; a composition comprising a propylene-ethylene copolymer; a shaped article thereof; and use of polyolefin.

First claim

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1 - 12 . (canceled) 13 . A process for the preparation of a catalyst system suitable for olefin polymerization, wherein the process comprises: A) providing said procatalyst obtainable via a process comprising: i) contacting a compound R 4 z MgX 4 2-z with an alkoxy- or aryloxy-containing silane compound to give a first intermediate reaction product, being a solid Mg(OR 1 ) x X 1 2-x , wherein: R 4 is the same as R 1 being a linear, branched or cyclic hydrocarbyl group independently selected from alkyl, alkenyl, aryl, aralkyl or alkylaryl groups, and one or more combinations thereof; wherein said hydrocarbyl group is substituted or unsubstituted, optionally comprises one or more heteroatoms and has between 1 and 20 carbon atoms; X 4 and X 1 are each independently selected from fluoride (F − ), chloride (Cl − ), bromide (Br − ) or iodide (I − ); and z is in a range of larger than 0 and smaller than 2, being 0<z<2; ii) optionally contacting the solid Mg(OR 1 ) x X 2-x obtained in step i) with at least one activating compound selected from activating electron donors and metal alkoxide compounds of formula M 1 (OR 2 ) v-w (OR 3 ) w or M 2 (OR 2 ) v-w (R 3 ) w , to obtain a second intermediate product; wherein M 1 is a metal selected from Ti, Zr, Hf, Al or Si; M 2 is a metal being Si; v is the valency of M 1 or M 2 ; R 2 and R 3 are each a linear, branched or cyclic hydrocarbyl group independently selected from alkyl, alkenyl, aryl, aralkyl, alkoxycarbonyl or alkylaryl groups, and one or more combinations thereof; wherein said hydrocarbyl group is substituted or unsubstituted, optionally contains one or more heteroatoms, and has between 1 and 20 carbon atoms; iii) contacting the first or second intermediate reaction product, obtained respectively in step i) or ii), with a halogen-containing Ti-compound and optionally an internal electron donor to obtain said procatalyst; and B) contacting said procatalyst with a co-catalyst and the at least one external electron donor that is diethylaminotriethoxysilane. 14 . The process according to claim 13 , wherein the process is essentially phthalate free. 15 . The process according to claim 13 , wherein the optional internal electron donor is present and is an aminobenzoate according to formula XI wherein R 80 , R 81 , R 82 , R 83 , R 84 , R 85 , and R 86 are independently selected from a group consisting of hydrogen, C 1 -C 10 straight and branched alkyl; C 3 -C 10 cycloalkyl; C 6 -C 10 aryl; and C 7 -C 10 alkaryl and aralkyl group; wherein R 81 and R 82 are each a hydrogen atom and R 83 , R 84 , R 85 and R 86 are independently selected from C 1 -C 10 straight and branched alkyl; C 3 -C 10 cycloalkyl; C 6 -C 10 aryl; and C 7 -C 10 alkaryl and aralkyl groups; wherein when one of R 83 and R 84 and one of R 85 and R 86 has at least one carbon atom, then the other one of R 83 and R 84 and of R 85 and R 86 is each a hydrogen atom; wherein R 87 is selected from hydrogen, methyl, ethyl, propyl, isopropyl, butyl, t-butyl, phenyl, benzyl, substituted benzyl and halophenyl groups; and wherein R 88 is selected from the group consisting of C 6 -C 10 aryl; and C 7 -C 10 alkaryl and aralkyl groups. 16 . The process according to claim 15 , wherein R 83 , R 84 , R 85 and R 86 are independently selected from C 1 -C 10 straight and branched alkyl and phenyl; and R 88 is a substituted or unsubstituted phenyl, benzyl, naphthyl, ortho-tolyl, para-tolyl or anisol group. 17 . The process according to claim 16 , wherein R 83, R 84 , R 85 and R 86 are are independently selected from methyl, ethyl, propyl, isopropyl, butyl, t-butyl, and phenyl groups; and R 88 is phenyl. 18 . The process according to claim 13 , wherein the optional internal electron donor is present, and is selected from 4-[benzoyl(methyl)amino]pentan-2-yl benzoate; 2,2,6,6-tetramethyl-5-(methylamino)heptan-3-ol dibenzoate; 4-[benzoyl (ethyl)amino]pentan-2-yl benzoate, 4-(methylamino)pentan-2-yl bis(4-methoxy)benzoate), 3-[benzoyl(cyclohexyl)amino]-1-phenylbutyl benzoate, 3-[benzoyl(propan-2-yl)amino]-1-phenylbutyl, 4-[benzoyl(methyl)amino]-1,1,1-trifluoropentan-2-yl, 3-(methylamino)-1,3-diphenylpropan-1-ol dibenzoate, 3-(methyl)amino-propan-1-ol dibenzoate; 3-(methyl)amino-2,2-dimethylpropan-1-ol dibenzoate, and 4-(methylamino)pentan-2-yl bis(4-methoxy)benzoate). 19 . The process according to claim 13 , wherein the one or more internal electron donor is present and is activated by an activator. 20 . The process according to claim 19 , wherein the activator is a benzamide according to formula X wherein: R 70 and R 71 are each independently selected from hydrogen or an alkyl, preferably an alkyl having between 1 and 6 carbon atoms; and R 72 , R 73 , R 74 , R 75 , R 76 are each independently selected from hydrogen, a heteroatom such as a halide, or a hydrocarbyl group selected from alkyl, alkenyl, aryl, aralkyl, alkoxycarbonyl or alkylaryl groups, and one or more combinations thereof. 21 . The process according to claim 19 , wherein R 70 and R 71 are each independently selected from hydrogen and an alkyl having between 1 and 6 carbon atoms. 22 . The process according to claim 21 wherein the activator is N,N-dimethylbenzamide. 23 . The process according to claim 20 , wherein the benzamide according to formula X is present in the procatalyst in an amount from 0.1 to 4 wt. % as determined using HPLC. 24 . A catalyst system obtained by the process of claim 13 . 25 . A process for preparing a polyolefin, comprising contacting at least one olefin with the catalyst system according to claim 24 . 26 . The process according to claim 25 , wherein the olefin is propylene or a combination of propylene and ethylene. 27 . A polyolefin obtained by the process for preparing a polyolefin according to claim 25 . 28 . The polyolefin according to claim 26 , wherein the polyolefin is a polypropylene or a propylene-ethylene copolymer. 29 . The process of claim 13 , wherein the optional internal electron donor is present and is an aminobenzoate according to formula XI wherein R 80 , R 81 , R 82 , R 83 , R 84 , R 85 , and R 86 are independently selected from a group consisting of hydrogen, C 1 -C 10 straight and branched alkyl; C 3 -C 10 cycloalkyl; C 6 -C 10 aryl; and C 7 -C 10 alkaryl and aralkyl group; wherein R 81 and R 82 are each a hydrogen atom and R 83 , R 84 , R 85 and R 86 are independently selected from C 1 -C 10 straight and branched alkyl; C 3 -C 10 cycloalkyl; C 6 -C 10 aryl; and C 7 -C 10 alkaryl and aralkyl groups; wherein when one of R 83 and R 84 and one of R 85 and R 86 has at least one carbon atom, then the other one of R 83 and R 84 and of R 85 and R 86 is each a hydrogen atom; wherein R 87 is selected from hydrogen, methyl, ethyl, propyl, isopropyl, butyl, t-butyl, phenyl, benzyl, substituted benzyl and halophenyl groups; and wherein R 80 is selected from the group consisting of C 6 -C 10 aryl; and C 7 -C 10 alkaryl and aralkyl groups; the one or more internal electron donor is activated by an activator, wherein the activator is a benzamide according to formula X

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What does patent US2016311950A1 cover?
A process for the preparation of a catalyst system for olefin polymerization, including: A) providing said procatalyst obtainable via a process comprising: i) contacting a compound R 4 z MgX 4 2-z with an alkoxy- or aryloxy-containing silane compound to give a first intermediate reaction product, ii) optionally contacting the solid product obtained in step i) with at least one activating c…
Who is the assignee on this patent?
Saudi Basic Ind Corp, Sabic Global Technologies Bv, Sabic Global Technologies Bv
What technology area does this patent fall under?
Primary CPC classification C08F210/06. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Oct 27 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).