Bimodal propylene polymers and sequential polymerization

Patent metadata

Field	Value
Publication number	US-9809664-B2
Application number	US-201615142268-A
Country	US
Kind code	B2
Filing date	Apr 29, 2016
Priority date	Jun 5, 2015
Publication date	Nov 7, 2017
Grant date	Nov 7, 2017

Abstract

This invention relates to high porosity (≧15%) and/or low pore diameter (PD<165 μm) propylene polymers and propylene polymerization processes using single site catalyst systems with supports having high surface area (SA≧400 m 2 /g), low pore volume (PV≦2 mL/g), a specific mean pore diameter range (PD=1-20 nm), and high average particle size (PS≧30 μm).

First claim

What is claimed is:

1. A process to polymerize propylene comprising:
(a) contacting monomer comprising propylene under polymerization conditions with a catalyst system comprising a single site catalyst precursor compound, an activator, and a support comprising an average particle size of more than 30 μm, a surface area of 400 m 2 /g or more, a pore volume of from 0.5 to 2 mL/g, and a mean pore diameter of from 1 to 20 nm (10 to 200 Å);
(b) polymerizing the propylene in (a) for a time period, A1 to form a first mode of propylene polymer comprising at least 50 mol % propylene;
(c) adding hydrogen or other chain transfer agent and optional comonomer to the polymerization after time period A1;
(d) then polymerizing the propylene in (a) in the presence of at least 1 mmol of the hydrogen or other chain transfer agent per mol of propylene for a time period, A2, wherein a concentration of the hydrogen or other chain transfer agent during time period A2 is greater than the concentration of the hydrogen or other chain transfer agent in time period A1 to form a second mode of the propylene polymer having a lower Mw with respect to the first mode; and
(e) forming a matrix of the propylene polymer, the matrix having a porosity, after time period A2, of 15% or more, as determined by mercury intrusion porosimetry.

2. The process of claim 1 , wherein the matrix after time period A2 has a median pore diameter less than 165 μm, as determined by mercury intrusion porosimetry.

3. The process of claim 1 , wherein time period A1 is at least as long as time period A2 and the concentration of the hydrogen or other chain transfer agent during time period A2 is at least three times greater than the concentration of the hydrogen or other chain transfer agent in time period A1.

4. The process of claim 1 , wherein the support has an average particle size of more than 50 μm.

5. The process of claim 1 , wherein the specific surface area is more than 650 m 2 /g and the mean pore diameter is less than 7 nm (70 Å).

6. The process of claim 5 , wherein the catalyst system has a bimodal particle size distribution.

7. The process of claim 6 , wherein the catalyst system comprises two modes: 1) a larger mode present at at least about 80 vol % having a particle size of 120 um or larger and 2) a smaller mode present at at least about 5 vol %, based on the total volume of the catalyst system.

8. The process of claim 6 , wherein the propylene polymer has a bimodal particle size distribution after time period A1 or after time period A2.

9. The process of claim 1 , wherein the specific surface area is less than 650 m 2 /g.

10. The process of claim 1 , further comprising polymerizing ethylene monomer comprising ethylene and from about 3 wt % to 75 wt % of one or more C 3 to C 20 alpha olefins in the presence of the propylene polymer matrix to fill pores in the matrix with a fill phase comprising from 15 to 80 wt % by total weight of the matrix and fill phase.

11. The process of claim 1 , wherein the support comprises agglomerates of primary particles.

12. The process of claim 1 , wherein the support comprises agglomerates of primary particles and the process further comprises fragmenting the agglomerates in (a) and dispersing catalyst sites in the propylene polymer matrix.

13. The process of claim 1 , wherein the activator comprises alumoxane.

14. The process of claim 1 , wherein the catalyst system further comprises a co-activator selected from the group consisting of: trialkylaluminum, dialkylmagnesium, alkylmagnesium halide, and dialkylzinc.

15. The process of claim 1 , wherein the contacting of the propylene monomer with the catalyst system during time period A1, time period A2, or a combination thereof, is carried out in the liquid slurry phase.

16. The process of claim 1 , wherein the polymerization conditions during time periods A1 and A2 comprise a pressure of from about 0.96 MPa (140 psi) to about 5.2 MPa (750 psi) and a temperature of from about 50° C. to 100° C.

17. The process of claim 1 , wherein the propylene monomer in (a) is essentially free of ethylene and C 4 to C 20 alpha olefins, and the propylene polymer formed is a propylene homopolymer.

18. The process of claim 1 , wherein the activator comprises alumoxane and non-coordinating anion.

19. The process of claim 1 , wherein the single site catalyst precursor compound is selected from precursor compounds I and II;
wherein precursor compound I is represented by the following formula:
(Cp) m R A n M 4 Q k

wherein:
each Cp is a cyclopentadienyl moiety or a substituted cyclopentadienyl moiety substituted by one or more hydrocarbyl radicals having from 1 to 20 carbon atoms;
R A is a structural bridge between two Cp moieties;
M 4 is a transition metal selected from groups 4 or 5;
Q is a hydride or a hydrocarbyl group having from 1 to 20 carbon atoms or an alkenyl group having from 2 to 20 carbon atoms, or a halogen;
m is 1, 2, or 3, with the proviso that when m is 2 or 3, each Cp is the same or different;
n is 0 or 1, with the proviso that n=0 when m=1; and
k is such that k+m is equal to the oxidation state of M 4 , with the proviso that if k is greater than 1, each Q is the same or different; and
wherein precursor compound II is represented by the following formula:
R A (CpR″ p )(CpR* q )M 5 Q r

wherein:
each Cp is a cyclopentadienyl moiety or substituted cyclopentadienyl moiety;
each R* and R″ is a hydrocarbyl group having from 1 to 20 carbon atoms and may the same or different;
p is 0, 1, 2, 3, or 4;
q is 1, 2, 3, or 4;
R A is a structural bridge between the Cp moieties imparting stereorigidity to the metallocene compound;
M 5 is a group 4, 5, or 6 metal;
Q is a hydrocarbyl radical having 1 to 20 carbon atoms or is a halogen;
r is s minus 2, where s is the valence of M 5 ;
wherein (CpR* q ) has bilateral or pseudobilateral symmetry; R* q is selected such that (CpR* q ) forms a fluorenyl, alkyl substituted indenyl, or tetra-, tri-, or dialkyl substituted cyclopentadienyl radical; and (CpR″ p ) contains a bulky group in one and only one of the distal positions;
wherein the bulky group is of the formula AR w v ; and
where A is chosen from group 4 metals, oxygen, or nitrogen, and R w is a methyl radical or phenyl radical, and v is the valence of A minus 1.

20. The process of claim 1 , wherein the single site catalyst precursor compound is represented by the formula:

wherein:
M is a group 4, 5 or 6 metal;
T is a bridging group;
each X is, independently, an anionic leaving group;
each R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , and R 13 is, independently, halogen atom, hydrogen, hydrocarbyl, substituted hydrocarbyl, halocarbyl, substituted halocarbyl, silylcarbyl, substituted silylcarbyl, germylcarbyl, substituted germylcarbyl substituent or a —NR′ 2 , —SR′, —OR, —OSiR′ 3 or —PR′ 2 radical, wherein R′ is one of a halogen atom, a C 1 -C 10 alkyl group, or a C 6 -C 10 aryl group.

21. The process of claim 20 , wherein at least one of R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , and R 13 is a cyclopropyl substitutent represented by the formula:

wherein each R′ in the cyclopropyls substituent is, independently, hydrogen,

Assignees

• Exxonmobil Chemical Patents Inc

Inventors

• Lubin Luo
• Holtcamp Matthew W
• Day Gregory S

Classifications

• C08F10/06 Primary

  Propene · CPC title

• C08F4/65916

  supported on a carrier, e.g. silica, MgCl2, polymer · CPC title

• C08F4/02

  Carriers therefor · CPC title

• C08F210/06

  Propene · CPC title

• C08F110/06 Primary

  Propene · CPC title