Process for the preparation of polyolefin-based graft copolymers comprising a first long chain branched polyolefin block and one or multiple polymer side chains

Patent metadata

Field	Value
Publication number	US-10717826-B2
Application number	US-201615781796-A
Country	US
Kind code	B2
Filing date	Nov 21, 2016
Priority date	Dec 9, 2015
Publication date	Jul 21, 2020
Grant date	Jul 21, 2020

Abstract

The present invention relates to a process for the preparation of polyolefin-based graft copolymers comprising a first long chain branched polyolefin block and one or multiple polymer side chains. The functionalized long chain branched polyolefin is produced via the copolymerization of an olefin monomer and an olefin bearing a main group metal hydrocarbyl functionality. The invention moreover relates to polyolefin obtained by said process ends. Subsequently the graft copolymers according to the invention can be produced for example by ring-opening polymerization of cyclic monomers or by transesterification of a preformed transesterifiable polymer, especially polyesters or polycarbonates. The invention moreover relates to polyolefin-based graft copolymers obtained by said process.

First claim

The invention claimed is:

1. A process for the preparation polyolefin-based graft copolymers comprising a first long chain branched polyolefin block and one or multiple polymer side chains, said process comprising the step of:
A) a polymerization step comprising copolymerizing at least one first type of olefin monomer and at least one second type of olefin monomer comprising a main group metal hydrocarbyl functionality according to Formula 1a:
R 100 (n-2) R 101 M n+ R 102   Formula 1a

using a catalyst system to obtain a polyolefin; wherein said catalyst system comprises a catalyst or catalyst precursor comprising a metal from Group 3-10 of the IUPAC Periodic Table of elements that can undergo chain transfer polymerization with the main group metal hydrocarbyl functionality of the second type of olefin monomer or that via a chain shuttling agent can undergo chain transfer polymerization with the main group metal hydrocarbyl functionality of the second type of olefin monomer, and optionally at least one of a co-catalyst or a scavenger, and
wherein further M is a main group metal; n is the oxidation state of M; R 100 , R 101 and R 102 of Formula 1a are each independently selected from the group consisting of a hydride, a C1-C18 hydrocarbyl group, or a hydrocarbyl group Q on the proviso that at least one of R 100 , R 101 and R 102 is a hydrocarbyl group Q, wherein hydrocarbyl group Q is according to Formula 1b:

wherein Z is bonded to M and Z is a C1-C18 hydrocarbyl group; R 105 optionally forms a cyclic group with Z; wherein R 103 and R 104 and R 105 are each independently selected from hydrogen or a hydrocarbyl group;
B) an oxidizing step comprising contacting said polyolefin obtained in step A) with at least one oxidizing agent to obtain a polyolefin having one or more pending oxidized functionalities; a
C) contacting said polyolefin obtained in step B) with at least one quenching agent to obtain a polyolefin having one or more pending polar functionalities, and
D) using the polyolefin having one or more pending polar functionalities obtained in step C) to obtain a graft copolymer by transesterification of a preformed transesterifiable polymer and/or by ring-opening polymerization of cyclic monomers.

2. A process according to claim 1 , wherein said oxidizing agent used in step B) is an oxidizing agent according to Formula I:
XY a Z 1 b Z 2 c    Formula I

wherein a is 1, b and c are each independently 0 or 1 and X, Y, Z 1 and Z 2 are independently selected from carbon, hydrocarbyl or heteroatom.

3. A process according to claim 1 , wherein the oxidizing agent used in step B) is selected from the group consisting of CO, CO 2 , CS 2 , COS, R 2 NCO, R 2 NCS, R 2 NCNR 3 , CH 2 ═C(R 2 )C(═O)OR 3 , CH 2 ═C(R 2 )(C═O)N(R 3 )R 4 , CH 2 ═C(R 2 )P(═O)(OR 3 )OR 4 , N 2 O, R 2 CN, R 2 NC, epoxide, aziridine, cyclic anhydride, R 3 R4C═NR 2 , R 2 C(═O)R 3 , ClC(═O)OR 2 and SO 3 .

4. A process according to claim 1 , wherein at least one of R 100 , R 101 and R 102 is a hydrocarbyl group Q and the remaining groups of R 100 , R 101 and R 102 are each a C1-C4 hydrocarbyl group or wherein two groups of R 100 , R 101 and R 102 are each a hydrocarbyl group Q and the remaining group of R 100 , R 101 and R 102 is a C1-C4 hydrocarbyl group or wherein all of R 100 , R 101 and R 102 are a hydrocarbyl group Q.

5. A process according to claim 1 , wherein the hydrocarbyl group Q according to Formula 1b attached to a main group metal is a linear α-olefin group or a cyclic unsaturated hydrocarbyl group.

6. A process according to claim 1 , wherein at least one type of olefin monomer comprises a main group metal hydrocarbyl functionality that is selected from the group consisting of bis(isobutyl)(5-ethylen-yl-2-norbornene) aluminum, di(isobutyl)(7-octen-1-yl) aluminum, di(isobutyl)(5-hexen-1-yl) aluminum, di(isobutyl)(3-buten-1-yl) aluminum, tris(5-ethylen-yl-2-norbornene) aluminum, tris(7-octen-1-yl) aluminum, tris(5-hexen-1-yl) aluminum, or tris(3-buten-1-yl) aluminum, ethyl(5-ethylen-yl-2-norbornene) zinc, ethyl(7-octen-1-yl) zinc, ethyl(5-hexen-1-yl) zinc, ethyl(3-buten-1-yl) zinc, bis(5-ethylen-yl-2-norbornene) zinc, bis(7-octen-1-yl) zinc, bis(5-hexen-1-yl) zinc, or bis(3-buten-1-yl) zinc.

7. A process according to claim 1 , wherein the catalyst system comprises the co-catalyst, and the co-catalyst is selected from the group consisting of TEA, DEAC, MAO, DMAO, MMAO, SMAO, optionally in combination with an aluminum alkyl.

8. A process according to claim 1 , wherein the metal catalyst or metal catalyst precursor used in step A) comprises a metal from Group 3-8 of the IUPAC Periodic Table of elements.

9. A process according to claim 8 , wherein said metal catalyst or catalyst precursor is a Ziegler-Natta catalyst and/or a C s -, C 1 -, or C 2 -symmetric zirconium metallocene.

10. A process according to claim 8 , wherein said metal catalyst or metal catalyst precursor is [Me 2 Si(C 5 Me 4 )N(tBu)]TiCl 2 , Me 2 Si(2-Me-4-Ph-Ind) 2 HfCl 2 , [C 5 Me 4 CH 2 CH 2 N(n-Bu) 2 ]TiCl 2 , bis(n-propyl-cyclopentadienyl)ZrCl 2 , bis(n-butyl-cyclopentadienyl)ZrCl 2 .

11. A process according to claim 1 , wherein the at least one type of olefin monomer used in step A) is selected from the group consisting of ethylene, propylene, 1-butene, 4-methyl-1-pentene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene, 1-undecene, 1-dodecene, 1-tridecene, 1-tetradecene, 1-pentadecene, 1-hexadecene, 1-heptadecene, 1-octadecene, cyclopentene, cyclohexene, norbornene, ethylidene-norbornene, and vinylidene-norbornene and one or more combinations thereof.

12. A process according to claim 1 , wherein an additional main group metal hydrocarbyl chain transfer agent is used in step A), and the additional main group metal hydrocarbyl chain transfer agent is selected from the group consisting of: hydrocarbyl aluminum, hydrocarbyl magnesium, hydrocarbyl zinc, hydrocarbyl gallium, hydrocarbyl boron, hydrocarbyl calcium and one or more combinations thereof.

13. A polyolefin-based graft copolymer comprising a first long chain branched polyolefin block and one or multiple polymer side chains obtained by a process according to claim 1 , the polyolefin-based graft copolymer having a number average molecular weight (M n ) between 500 and 1,000,000 g/mol and having a polydispersity index (Ð) of between 1.1 and 10.0 and wherein said polyolefin block has a branching number determined by NMR of 0.2 to 10 per 10000 carbon atoms or of 50 to 3500 per 10000 carbon atoms.

14. A polyolefin-based graft copolymer according to claim 13 , wherein the polymer side chain(s) comprise at least one monomer that is different from the monomer(s) of the first long chain branched polyolefin block and/or wherein the grafts are comprise ester and/or carbonate functionalities.

15. A polyolefin-based graft copolymer according to claim 13 , the polymer side chain(s) having a number average molecular weight (M n ) between 500 and 1,000,000 g/mol.

16. A process according to claim 1 , wherein the oxidizing agent used in step B) is selected from the group consisting of N 2 O, CO 2 and SO 3 .

17. A process according to claim 1 , wherein the hydrocarbyl group Q according to Formula 1b attached to a main group metal is but-3-en-1-yl, pent-4-en-1-yl, hex-5-en-1-yl, hept-6-en-1-yl or oct-7-en-1yl, 5-ethylenebicyclo[2.2.1]hept-2-ene or 5-propylenebicyclo[2.2.1]hept-2-ene.

18. A process accordin

Assignees

• Sabic Global Technologies Bv

Inventors

• Duchateau Robbert
• Bouyahyi Miloud
• Jasinska-Walc Lidia

Classifications

• C08F2420/02

  Cp or analog bridged to a non-Cp X anionic donor · CPC title

• C08G63/823

  for the preparation of polylactones or polylactides · CPC title

• C08F8/06

  Oxidation · CPC title

• C08F2810/50

  wherein the polymer is a copolymer and the modification is taking place only on one or more of the monomers present in minority · CPC title

• C08F210/02

  Ethene · CPC title