Procatalyst for polymerization of olefins

Patent metadata

Field	Value
Publication number	US-10246529-B2
Application number	US-201615541088-A
Country	US
Kind code	B2
Filing date	Jan 20, 2016
Priority date	Jan 21, 2015
Publication date	Apr 2, 2019
Grant date	Apr 2, 2019

Abstract

The invention relates to a procatalyst for polymerization of olefins. The invention also relates to a process for preparing said procatalyst. Furthermore, the invention is directed to a catalyst system for polymerization of olefins comprising the said procatalyst, a co-catalyst and optionally an external electron donor; a process of preparing polyolefins by contacting an olefin with said catalyst system and to polyolefins obtained or obtainable by said process. The invention also relates to the use of said procatalyst in the polymerization of olefins.

First claim

The invention claimed is:

1. A process for preparing a procatalyst for preparing a catalyst composition for olefin polymerization, said process comprising the steps of:
ia) contacting a Grignard reagent comprising R 4 z MgX 4 2-z and an alkyl magnesium compound MgR 4′ 2 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 and R 4 ′ are the same as R 1 being a linear, branched or cyclic hydrocarbyl group independently selected from the group consisting of alkyl, alkenyl, aryl, aralkyl, alkoxycarbonyl, alkylaryl groups, and one or more combinations thereof; wherein said hydrocarbyl group is substituted or unsubstituted, and optionally contains one or more heteroatoms;
X 4 and X 1 are each independently selected from the group consisting of fluoride (F—), chloride (Cl—), bromide (Br—) or iodide (I—);
x is in a range of larger than 0 and smaller than 2, being 0<x<2; and
z is in a range of larger than 0 and smaller than 2, being 0<z<2;

ib) precipitating the solid Mg(OR 1 ) x X 1 2-x obtained in step ia) by contacting it with an tetrahalogensilane, SiX 4′ 4 , wherein X 4′ is each independently selected from the group consisting of fluoride (F—), chloride (Cl—), bromide (Br—) or iodide (I—), to obtain a solid support;
ii) optionally contacting the solid support obtained in step ib) with at least one activating compound selected from the group consisting of activating electron donors and metal alkoxide compounds of formula M 1 (OR 2 ) v-w (OR 3 ) w and M 2 (OR 2 ) v-w (R 3 ) w , to obtain a second intermediate reaction product; wherein:
M 1 is a metal selected from the group consisting of Ti, Zr, Hf, Al or Si;
M 2 is a metal being Si;
v is the valency of M 1 or M 2 ;
w is smaller than v;
R 2 and R 3 are each a linear, branched or cyclic hydrocarbyl group independently selected from the group consisting of alkyl, alkenyl, aryl, aralkyl, alkoxycarbonyl, alkylaryl groups, and one or more combinations thereof; wherein said hydrocarbyl group is substituted or unsubstituted, and optionally contains one or more heteroatoms;

iii) contacting the first or second intermediate reaction product obtained in step ib) or ii) respectively, with a halogen-containing titanium compound and either an activator or an internal electron donor to obtain a third intermediate reaction product;
iv) optionally modifying the third intermediate reaction product obtained in step iii) with a modifier having the formula MX 3 , wherein M is a metal selected from the Group 13 metals and transition metals of the IUPAC periodic table of elements, and wherein X is a halide, to yield a modified intermediate reaction product; and
v) contacting said third intermediate reaction product obtained in step iii) or said modified intermediate reaction product obtained in step iv) with a halogen-containing titanium compound and in the case that in step iii) an activator was used an internal donor to obtain the procatalyst.

2. The process according to claim 1 , wherein the activator added during step iii) is selected from the group consisting of alkyl benzoate, benzamide, and monoester.

3. The process according to claim 1 , wherein the alkyl magnesium compound used in step ia) is dibutylmagnesium.

4. The process according to claim 1 , wherein the Grignard reagent used in step ia) is butyl magnesium chloride.

5. The process according to claim 1 , wherein the Grignard reagent used in step ia), and the halogen-containing titanium compound used in step iii) and step v) are used in such amounts that the resulting procatalyst comprises in wt. % based on the total weight of the procatalyst:magnesium: from 15 to 24; titanium: from 1 to 4.

6. The process according to claim 1 , wherein step ii) is carried out using a combination of an alcohol and a tetra alkoxy titanium compound as the activating compounds.

7. The process according to claim 1 , wherein the ratio between the alkyl magnesium and Grignard reagent is between 1:1 and 1:4.

8. The process according to claim 1 , wherein a ratio of an amount of said tetrahalogensilane compound to the combined amount of magnesium of the Grignard reagent and the compound MgR 4′ 2 is 0.2 to 5.

9. A procatalyst obtained by the process according to claim 1 , said procatalyst comprising a titanium catalyst supported on a solid magnesium-containing support characterized in that the procatalyst comprises in wt. % based on the total weight of the procatalyst:magnesium: from 15 to 24; and titanium: from 1 to 4.

10. The procatalyst according to claim 9 , wherein the procatalyst comprises in wt. % based on the total weight of the procatalyst:magnesium: from 19.0 to 19.5; and/or titanium: from 1.5 to 3.5.

11. A catalyst system for olefin polymerization comprising the procatalyst according to claim 9 , a co-catalyst, and optionally an external electron donor.

12. The catalyst system according to claim 11 , wherein the co-catalyst is an organometallic compound containing a metal from group 1, 2, 12 or 13 of the Periodic System of the Elements.

13. A process of preparing a polyolefin, the process comprising contacting at least one olefin with a polymerization catalyst system according to claim 11 .

14. The process according to claim 1 , wherein
the activator added during step iii) is selected from the group consisting of alkyl benzoate, benzamide, and monoester;
the alkyl magnesium compound used in step ia) is dibutylmagnesium;
the Grignard reagent used in step ia) is butyl magnesium chloride;
the Grignard reagent used in step ia), and the halogen-containing titanium compound used in step iii) and step v) are used in such amounts that the resulting procatalyst comprises in wt. % based on the total weight of the procatalyst:magnesium: from 15 to 24; titanium: from 1 to 4;
step ii) is carried out using a combination of an alcohol and a tetra alkoxy titanium compound as the activating compounds;
the ratio between the alkyl magnesium compound and Grignard reagent is between 1:1 and 1:4;
a ratio of an amount of said tetrahalogensilane compound to the combined amount of magnesium of the Grignard reagent and the compound MgR 4′ 2 is 0.2 to 5.

15. The process according to claim 14 , wherein
X 4 and X 1 have from 1 to 20 carbon atoms;
X 4 , X 1 , and X 4′ are each chloride;
R 2 and R 3 each have from 1 to 20 carbon atoms;
step v) is carried out at least two times;
the activator is ethyl benzoate;
the Grignard reagent used in step ia), and the halogen-containing titanium compound used in step iii) and step v) are used in such amounts that the resulting procatalyst comprises in wt. % based on the total weight of the procatalyst:magnesium: from 18.0 to 19.5; titanium: from 1.5 to 3.5;
step ii) is carried out using an combination of ethyl alcohol and tetraethoxy titanium as the activating compounds; and
said tetrahalogensilane compound is present in respect of the amount of magnesium of the Grignard reagent and the compound MgR 4′ 2 in a ratio of 0.5 to 1.

16. A catalyst system for polymerization of ethylene or a mixture of ethylene and propylene, the method comprising:
a procatalyst obtained by the method of claim 14 , said procatalyst comprising a titanium catalyst supported on a solid magnesium-containing support characterized in that the procatalyst comprises in wt. % based on the total weight of the procatalyst:magnesium: from 15 to 24; and titanium: from 1 to 4;
a co-catalyst, wherein the co-catalyst is an organometallic compound containing a metal from group 1, 2, 12 or 13

Assignees

• Sabic Global Technologies Bv

Inventors

• Padmanabhan Sudhakar R
• Al-Bahily Khalid Abdullah

Classifications

• C08F210/06

  Propene · CPC title

• C08F110/06

  Propene · CPC title

• C08F10/06 Primary

  Propene · CPC title

• C07F7/28 Primary

  Titanium compounds · CPC title

• C08F210/02

  Ethene · CPC title