WO2017097570A1

WO2017097570A1 - Process for the preparation of polyolefin-based graft copolymers comprising a first long chain branched polyolefin block and one or multiple polymer side chains

Info

Publication number: WO2017097570A1
Application number: PCT/EP2016/078302
Authority: WO
Inventors: Robbert Duchateau; Miloud BOUYAHYI; Lidia JASINSKA-WALC
Original assignee: Sabic Global Technologies B.V.
Priority date: 2015-12-09
Filing date: 2016-11-21
Publication date: 2017-06-15

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.

Description

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

Description

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 according to Formula 1 a. 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.

Background

The present invention relates to the preparation of polyolefin-based graft copolymers comprising a first long chain branched polyolefin block and one or multiple polymer side chains, the intermediate products and the processes to obtain these products.

Commercially available polyethylene and polypropylene prepared using standard procedures with Ziegler-Natta or single-site catalysts have a predominantly linear molecular structure. Although linear polyolefins have many desirable physical properties, they show a variety of melt processing shortcomings, especially the single- site prepared ones having narrow molecular weight distributions , which typically have a low melt strength. Low melt strength is a problem because it causes local thinning in melt thermoforming, relative weakness in large-part blow molding and flow instabilities in co-extrusion of laminates.

One way of overcoming the shortcomings of li near polyolefins is by means of long chain branching, viz. the provision of polymer side chains extending from the polyolefin backbone. 9

Despite their ubiquitous presence in our society, polyolefins such as polyethylene and polypropylene are not appropriate for several applications as a consequence of their inherently nonpolar character. This nonpolar character is the reason for the poor adhesion, printability and compatibility that can restrict their efficacy. Hence, it is further desirable to prepare polyolefins bearing for example polar groups so to ensure a good adhesion and printability.

In the prior art copolymers have thus been prepared and considered to overcome the shortcomings of polyolefins mentioned above. However, the preparation of these copolymers is often complicated and cumbersome. Moreover, most preparation methods lack flexibility.

The present invention is directed towards an easy, catalyst-compatible, relatively inexpensive and safe process that can be used for large scale preparation of polyolefin- based graft copolymers comprising a first long chain branched polyolefin block and one or multiple polymer side chains.

Summary of the invention

In a first aspect, 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, said process comprising the step of:

A) a polymerization step comprising copolymerizing at least one first type of olefin monomer, preferably selected for example from ethylene or propylene, and at least one second type of olefin monomer comprising a main group metal hydrocarbyl functionality according to Formula 1 a: R^{1 00}(_n-2) ¹⁰¹ Mⁿ⁺R¹⁰² using a catalyst system to obtain a polyolefin; wherein said catalyst system comprises a co-catalyst and/or a scavenger and a catalyst or catalyst precursor comprising a metal from Group 3-10 of the l UPAC 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 ό monomer and

wherein further M is a main group metal; n is the oxidation state of M; R¹⁰⁰, R¹⁰¹ and R¹⁰² of Formula 1 a are each independently selected from the group consisting of a hydride, a C1 -C18 hydrocarbyl group, a halide, an alkoxide, an amide, a thiolate or a hydrocarbyl group Q on the proviso that at least one of R¹⁰⁰, R¹⁰¹ and R¹⁰² is a hydrocarbyl group Q, wherein hydrocarbyl group Q is according to Formula 1 b:

(Formula 1 b)

wherein Z is bonded to M and Z is a C1 -C18 hydrocarbyl group; R¹⁰⁵ optionally forms a cyclic group with Z; wherein R¹⁰³ and R¹⁰⁴ and R¹⁰⁵ are each independently selected from hydrogen or a hydrocarbyl group; and at least one step of:

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; and/or

C) using the polyolefin having one or more pending oxidized functionalities obtained in step B) to obtain a graft copolymer by transesterification of a preformed transesterifiable polymer and/or by ring-opening polymerization of cyclic monomers, especially cyclic esters (lactones) and/or cyclic carbonates. A polyolefin having one or more pending oxidized functionalities may be a polyolefin having a backbone preferably for example made of ethylene or propylene as well as of an olefin monomer comprising a main group metal hydrocarbyl functionality, as produced in step A), which has being subjected to an oxidative treatment in step B). The metal hydrocarbyl functionality of the second monomer can function as a chain transfer agent, giving rise to coordinative chain transfer polymerization. As a results of this, long chain branched polymers might be obtained having main group metal hydrocarbyl functionalities at the chains/branches. Since the long chain branches are actually growing chains as a result of the chain transfer process, they can also incorporate more of the second type of monomer, which will result in branches-on- branches structures. The second type of olefin monomer comprising a main group metal hydrocarbyl functionality can thereby comprise a spacer, like for example a substituted and/or unsubstituted alkyl chain and/or bridged or unbridged, substituted and/or unsubstituted, cyclic hydrocarbon , linking the olefin and the main group metal hydrocarbyl functionality. The second type of olefin monomer comprising a main group metal hydrocarbyl functionality can thereby comprise bridged or unbridged, substituted and/or unsubstituted, cyclic hydrocarbon as a spacer for example when a reactive cyclic olefin, especially for example a norbornene derivative comprising a main group metal hydrocarbyl functionality is used as the second type of olefin monomer.

A long chain branch can also preferably for example comprise between >100 to 100,000,000 carbon atoms, preferably between 500 to 10,000,000 carbon atoms, even more preferred between 1000 to 1 ,000,000 carbon atoms, more preferred between 10,000 to 500,000 carbon atoms, more preferred between 20,000 to 200,000 carbon atoms, preferably in the backbone, of the long chain branch. A long chain branch can also preferably for example be long enough to lead to entanglement phenomena, preferably involving the long chain branch.

Pending oxidized functionality may mean a functionality that preferably comprises at least one heteroatom that is different from carbon and hydrogen, preferably oxygen. Such a heteroatom may thereby be preferably more electronegative than carbon and/or hydrogen.

A heteroatom may be preferably for example selected from Group 14, 15, 16 or 17 of the l UPAC Periodic Table of the Elements and can as used in the present description for example especially mean a hetero atom selected from Si, Ge, Sn [Group 14], N, P, As, Sb, Bi [Group 15], O, S, Se, Te [Group 16] or halogens [Group 17].

Hydrocarbyl as used in the present description may means: a substituent containing hydrogen and/or carbon atoms; it may for example be a hydride or a linear, branched or cyclic saturated or unsaturated aliphatic substituent, such as for example alkyl, alkenyl, alkadienyl and alkynyl; alicyclic substituent, such as cycloalkyl, cycloalkadienyl cycloalkenyl; aromatic substituent or aryl, such as for example monocyclic or polycyclic aromatic substituent, as well as combinations thereof, such as alkyl-substituted aryls and aryl-substituted alkyls. It may be substituted with one or more non-hydrocarbyl, heteroatom-containing substituents or heteroatoms. Hence, when in the present description hydrocarbyl is used it can also mean a substituted hydrocarbyl, unless stated otherwise. Included in the term "hydrocarbyl" are also perfluorinated hydrocarbyls wherein all hydrogen atoms are replaced by fluorine atoms. A hydrocarbyl may moreover for example be present as a group on a compound (hydrocarbyl group) or it may be present as a ligand on a metal (hydrocarbyl ligand). Alkyl as used in the present description means: a group consisting of carbon and hydrogen atoms having only single carbon-carbon bonds. An alkyl group may be straight or branched, un-substituted or substituted. It may contain aryl substituents. It may or may not contain one or more heteroatoms. Aryl as used in the present description means: a substituent derived from an aromatic ring. An aryl group may or may not contain one or more heteroatoms. An aryl group also encloses substituted aryl groups wherein one or more hydrogen atoms on the aromatic ring have been replaced by hydrocarbyl groups. Hydride as used in the present description may mean: a hydrogen anion bonded to a metal.

In an embodiment, at least one of R¹⁰⁰, R¹⁰¹ and R¹⁰² of Formula 1 a can be a hydrocarbyl group Q and the remaining groups of R¹⁰⁰, R¹⁰¹ and R¹⁰² are each a C1 - C18 hydrocarbyl group, preferably a C1 -C10 hydrocarbyl group or wherein two groups of R¹⁰⁰, R¹⁰¹ and R¹⁰² are each a hydrocarbyl group Q and the remaining group of R¹⁰⁰, R¹⁰¹ and R¹⁰² is a C1 -C18 hydrocarbyl group, preferably C1 -C10 hydrocarbyl group, further preferred a C1 -C4 hydrocarbyl group, or wherein all of R¹⁰⁰, R¹⁰¹ and R¹⁰² are a hydrocarbyl group Q. Expressions like for example "C1 -C4" or "C1-C16" and similar formulations may refer to a range regarding a number of carbon atoms, here for example respectively from 1 to 4 or from 1 to 16 carbon atoms.

In an embodiment, a second type of olefin monomer comprising a main group metal hydrocarbyl functionality can be 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. A cyclic unsaturated hydrocarbyl group can thereby lead for example to a high reactivity. I n an embodiment, the catalyst or catalyst precursor used in step A) may comprise a metal from Groups 3-1 0 of the l U PAC Periodic Table of elements, more preferably from Groups 3-8 from Groups 3-6 and/or wherein the metal catalyst or metal catalyst precursor used in step A) comprises a metal selected from the group consisting for example of Ti, Zr, Hf, V, Cr, Fe, Co, N i, Pd, preferably Ti, Zr or Hf.

I n an embodiment, said catalyst can be a Ziegler-Natta catalyst, such as for example titanium-magnesium and aluminum based Ziegler-Natta catalysts, especially obtained for example by reacting a titanium alkoxy with a magnesium alkoxy and subsequently reaction the reaction product with an aluminum alkyl halide, or a catalyst based on a Group 4 metal , which can especially be for example a metallocene, half-metallocene or a post-metallocene and/or a single-site catalyst.

In an embodiment, a catalyst precursor can be for example a C₃-, C or C2- symmetric zirconium or hafnium metallocene, preferably an indenyl substituted zirconium or hafnium dihalide, more preferably a bridged bis-indenyl zirconium or hafnium dihalide, even more preferably rac-dimethyl silyl bis-indenyl zirconium or hafnium dichloride (rac- Me2Si(lnd)2ZrCl2 and rac-Me2Si(lnd)2HfCl2, respectively), or rac-dimethylsilyl bis-(2-methyl- 4-phenyl-indenyl) zirconium or hafnium dichloride (rac-Me2Si(2-Me-4-Ph-lnd)2ZrCl2 and rac-Me₂Si(2-Me-4-Ph-l nd)2HfCl2, respectively).

I n an embodiment, said catalyst precursor can be for example a so-called half- metallocene, or constrained geometry catalyst, even more preferably, C₅Me₅[(C6Hi i )₃P=N]TiCl2, [Me₂Si(C₅Me₄)N(tBu)]TiCl2, [C₅Me₄(CH₂CH₂N Me2]TiCl2. In an embodiment, said catalyst can be for example a so-called post-metallocene, preferably [Et₂NC(N(2,6-i Pr2-C6H₃)]TiCl3 or [N-(2,6-di(l-methylethyl)phenyl)amido)(2- isopropylphenyl)(a-naphthalen-2-diyl(6-pyridin-2-diyl)methane)]hafnium dimethyl . For example oxygen, ozone or oxygen-containing gas mixtures such as air or synthetic air or mixtures of oxygen with other gases can be used as oxidizing agents in step B).

Moreover, at least one safe oxidation agent can for example be used in step B). In an embodiment, at least safe oxidizing agent according to the invention used in step B) can for example be preferably selected from the group consisting of CO, CO2, CS2, COS, N2O and SO3, preferably, N2O, CO2 and SO3 or mixtures of at least two or more thereof, even more preferably CO2. A safe oxidizing agent in the sense of the present invention, can thereby be for example be an compound where at least one oxygen is bound at least one other atom then oxygen and/or a compound comprising at least one nitrogen-carbon CN double or triple bond. Using safe oxidants according to the present invention thereby allows reducing the process risk (especially for example the risk of fire and explosions) associated with the use of the oxidizing agent, so as to be able to easily scale up the reactions and/or use high pressures.

The inventors could thereby surprisingly show that the use of safe oxidizing agents did lead to an oxidation and/or functionalization yield equal or higher than with gaseous oxygen or oxygen containing gas mixtures could be obtained. Oxidation and/or functionalization yield can thereby preferably for example be > 50 %, preferred > 60 %, further preferred > 70 % or even further preferred > 80 %.

The present invention will be described in more detail below.

Detailed description of the invention

The present invention concerns the copolymerization of an olefin monomer, preferably ethylene or propylene, and at least one second type olefin monomer, preferably also 0 olefin, containing a main group metal hydrocarbyl functionality, to obtain long chain branches via chain transfer polymerization. Subsequently the graft copolymers according to the invention can be produced for example by ring-opening polymerization (ROP) of cyclic monomers and/or by transesterification of a preformed transesterifiable polymer, especially polyesters or polycarbonates. A transesterifiable polymer in the sense of the invention may thereby be for example a polyester, a polycarbonate, a polyamide, a polyurethane, a polyurea, a random or block polycarbonate- ester), poly(carbonate-ether), poly(ester-ether), poly(carbonate-ether-ester), poly(ester- amide), poly(ester-ether-amide), poly(carbonate-amide), poly(carbonate-ether-amide), poly(ester-urethane), poly(ester-ether-urethane), poly(carbonate-urethane), poly(carbonate-ether-urethane), poly(ester-urea), poly(ester-ether-urea), polycarbonate- urea), poly(carbonate-ether-urea), poly(ether-amide), poly(amide-urethane), poly(amide- urea), poly(urethane-urea) or one or more combination(s) thereof. The invention moreover relates to polyolefin-based graft copolymers obtained by said process. This can for example be used for the preparation of polyolefins having pending oxidized functionalities via an additional oxidation step.

Thus, it can be said that the intermediate that is desired in the present invention is a polyolefin having one or multiple preferably long chain branches. The copolymer obtained in step A) can thereby be oxidized and/or optionally subsequently quenched to produce the desired end product.

The present invention uses an olefin-comprising main group metal hydrocarbyl as comonomer. In other words, the olefin-comprising main group metal hydrocarbyl can be, for example, an alkene-comprising aluminum hydrocarbyl or an alkene-comprising zinc hydrocarbyl.

Step A):

The first step in the process according to the present invention is the preparation of a polyolefin having one or multiple main group metal functionalized long chain branches by polymerizing at least one first type of olefin monomer, preferably a a-olefin, and at least one second type of olefin monomer, preferably an oolefin, comprising a main group metal hydrocarbyl functionality, which functionalities as a chain transfer agent, with a metal catalyst that might undergo chain transfer polymerization with the main group metal hydrocarbyl functionality of the second type of olefin monomer either with or without chain shuttling agent, optionally a co-catalyst, optionally a scavenger and optionally one or more additional chain transfer agents and/or chain shuttling agents. In an embodiment, said main group metal hydrocarbyl functionality or a corresponding functionality can for example be an alkenyl-comprising aluminum hydrocarbyl or a corresponding functionality.

The second type of olefin monomer can comprise a main group metal hydrocarbyl functionality, which can for example be a reactive electrophilic metal group, which functionalities as a chain transfer agent. The metal hydrocarbyl functionality of the second monomer can function as a chain transfer agent, giving rise to coordinative chain transfer polymerization. As a results of this, long chain branched polymers might be obtained having main group metal hydrocarbyl functionalities at the chains/branches. Since the long chain branches are actually growing chains as a result of the chain transfer process, they can also incorporate more of the second type of monomer, which will result in branches-on-branches structures. The resulting polyolefin can have one or multiple long chain branches comprising at least one reactive electrophilic metal functionality, preferably for example at the end of the long chain branch(es). In other words, said product is a long chain branched polyolefin that is functionalized on at least one of its long chain branches with a main group metal.

Main group metal as used in the present description can refer to/mean: a metal that is of a main group, namely an element of groups 1 , 2, and 13-15 of the period table or zinc. In other words, metals of:

^* Group 1 : lithium (Li), sodium (Na), and potassium (K)

^* Group 2: beryllium (Be), magnesium (Mg), and calcium (Ca)

^* Group 13: boron (B), aluminum (Al), galliu m (Ga), and indium (In)

^* Group 14: germanium (Ge), and tin (Sn)

^* Group 15: antimony (Sb), and bismuth (Bi) of the l UPAC Periodic Table of elements main group metals also include for the context of the present invention zinc (Zn).

During the polymerization reaction according to step A) at least one olefin comprising a main group metal hydrocarbyl functionality (being for example a main group metal atom bearing one or more hydrocarbyl and/or hydride groups and at least one alkenyl group) is used. The product obtained in step A) is then a polyolefin having one or multiple main group metal-functionalized long chain branches (being a long chain branched polyolefin that is functionalized on at least one of its long chain branches with a main group metal). This is considered to be the main product of step A), which is an intermediate product in the process according to the present invention.

The catalyst system used in step A) comprises: i) a Group 3-10, preferably Group 3-8 and more preferably Group 3-6, metal catalyst or metal catalyst precursor as well as optionally one or more of ii) a co-catalyst, iii) a scavenger and/or iv) optionally one or more chain transfer agents and/or chain shuttling agents.

According to the present invention, the catalyst can be selected, preferably so that it may lead to an interaction, especially to chain transfer, preferably without poisoning, with the main group metal hydrocarbyl functionality of the second type of olefin monomer. A catalyst that does lead to an interaction and/or to chain transfer polymerization may thereby preferably for example be a catalyst that does lead to interaction products detectable by N MR and/or to chain transfer products detectable by N MR and/or viscosity measurements. An example of a selection made in that way, may be the selection of a catalyst comprising zirconium (Zr) or titanium (Ti) as the metal, for example rac-Me2Si(l nd)2ZrCl2, and of a main group metal hydrocarbyl functionality comprising aluminum (Al) as the metal for the second type of olefin monomer, since it is known that such a catalyst in the presence of a chain shuttling agent, preferably diethyl zinc, will lead to chai n transfer polymerization with an aluminum hydrocarbyl functionality. In the sense of the present invention, poisoning may thereby for example a poisoning that may reduce catalyst activity by at least 50 %, preferably by at least 25 %, further preferred by at least 20 %, even further preferred by at least 15 %, even further preferred by at least 10 %, even further preferred by at least 5 %, even further preferred by at least 3 %, even further preferred by at least 1 %, even further preferred by at least 0.5 %. Moreover, chain transfer polymerization in the sense of the present invention may thereby for example be a chain transfer polymerization that accounts for at least 50 %, preferably by at least 25 %, further preferred by at least 20 %, even further preferred by at least 15 %, even further preferred by at least 10 %, even further preferred by at least 5 %, even further preferred by at least 3 %, even further preferred by at least 1 %, even further preferred by at least 0.5 % of the polymer material produced by polymerization according to the process of the present invention.

This may preferably allow the formation of polymers with long chain branches by polymerizing the olefins of the at least two comonomers with the catalyst used .

Metal catalyst as used in the present description may mean: a catalyst providing the catalytic reaction, wherein said catalyst comprises at least one metal center that forms the active site. In the context of the present invention a "metal catalyst" is the same as a "transition metal catalyst" wherein the metal is a transition metal.

Metal catalyst or a metal catalyst precursor according to the invention may be for example a single-site catalyst or Ziegler-Natta catalyst.

Catalyst precursor as used in the present description may mean: a compound that upon activation forms the active catalyst. Single-site catalyst as used in the present description may mean especially for example: a metal catalyst or catalyst precursor that contains exclusively one type of active site. A single-site catalyst can thereby be a metallocene, half-metallocene or post-metallocene. Metallocene as used in the present description may mean: a metal catalyst or catalyst precursor typically consisting of two substituted cyclopentadienyl (Cp) ligan ds bound to a metal active site. Half-metallocene as used in the present description may for example mean: a metal catalyst or catalyst precursor typically consisting of one substituted cyclopentadienyl (Cp) ligand bound to a metal active site. Post-metallocene as used in the present description may mean especially for example: a metal catalyst that contains no substituted cyclopentadienyl (Cp) ligands, but may contains one or more anions bound to the metal active site, typically via a heteroatom.

Ziegler-Natta catalyst as used in the present description means: a transition metal- containing solid catalyst compound comprises a transition metal halide selected from itanium halide, chromium halide, hafnium halide, zirconium halide, and vanadium halide, supported on a metal or metalloid compound (e.g. a magnesium compound or a silica compound). An overview of such catalyst types is for example given by T. Pullukat and R. Hoff in Catal. Rev. - Sci. Eng. 41 , vol. 3 and 4, 389-438, 1999. The preparation of such a procatalyst is for example disclosed in W096/32427 A1 .

Transition metal as used in the present description may mean: a metal from any of the Groups 3-10 of the lUPAC Periodic Table of elements or in other words a Group 3 metal, a Group 4 metal, a Group 5 metal, a Group 6 metal, a Group 7 metal, a Group 8 metal, a Group 9 metal or a Group 10 metal.

Co-catalyst as used in the present description may mean a compound that activates the catalyst precursor to obtain the active catalyst. In an embodiment, the co-catalyst can be selected for example from the group consisting of MAO, DMAO, MMAO, SMAO, possibly in combination with aluminum alkyls, for example triisobutyl aluminum, and the combination of an aluminum alkyl, for example triisobutyl aluminum, and fluorinated aryl borane or fluorinated aryl borate. In an embodiment, the co-catalyst can be selected for example from aluminum alkyls and aluminum alkyl halides, such as for example triethyl aluminum (TEA) or diethyl aluminum chloride (DEAC). In an embodiment, the scavenger can be selected for example from the group consisting of trialkyl aluminum, for example triisobutyl aluminum, MAO, DMAO, MMAO, SMAO. Scavenger as used in the present description may mean a compound that scavenges impurities, especially protic and heteroatom containing compounds, such as for example water, alcohols or acids, from the reaction medium prior and during the polymerization process. The co-catalyst thereby also function for example as scavenger.

Olefins suitable for use in step A)

Examples of suitable monomers include linear or branched a-olefins. Said olefins preferably have between 2 and 30 carbon atoms, more preferably between 2 and 20 carbon atoms. Preferably, one or more of the following are used: 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, 1 -cyclopentene, cyclohexene, norbornene, ethylidene-norbornene, and vinylidene-norbornene and one or more combinations thereof. In addition, a combination of ethylene and/or propylene on the one and one or more other olefins on the other hand is also possible. Substituted analogues of the monomers discussed above may also be used, e.g. substituted by one or more halogens. In addition aromatic monomers can be used according to the present invention. It is also possible to use a combination of two or more olefins. Main group hydrocarbyl functionality

The present invention uses at least one olefin monomer comprising a main group hydrocarbyl functionality. The present invention may for example also use said monomer in combination with other main group metal chain transfer agents, for example, zinc and/or magnesium and/or calcium and/or boron and/or aluminum and/or gallium hydrocarbyl/hydride chain transfer agents.

The olefin monomer comprising a main group metal hydrocarbyl functionality used in the present invention has a structure according to Formula 1 a: R¹⁰V₂)R¹⁰¹ Mⁿ⁺R¹⁰²

Formula 1 a wherein: M is a main group metal; n is the oxidation state of M; R¹⁰⁰, R¹⁰¹ and R¹⁰² 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 R¹⁰⁰, R¹⁰¹ and R¹⁰² is hydrocarbyl group Q. Wherein hydrocarbyl group Q is according to Formula 1 b:

Formula 1 b wherein Z is bonded to M and is a C1 -C18 hydrocarbyl group; R¹⁰⁵ optionally forms a cyclic group with Z; wherein R¹⁰³ and R¹⁰⁴ and R¹⁰⁵ are each independently selected from hydrogen or hydrocarbyl;

In an embodiment, hydrocarbyl group Q is an a-olefin wherein Z is bonded to the main group metal, Z is a C1-C18 hydrocarbyl spacer group, R¹⁰³ R¹⁰⁴ and R¹⁰⁵are each hydrogen, said hydrocarbyl group Q being according to Formula 1 c:

Formula 1 c

In an embodiment, hydrocarbyl group Q is an alkene wherein Z is bonded to the main group metal, Z is a C1 -C18 hydrocarbyl spacer group, R¹⁰³ and R¹⁰⁴ are independently hydrogen or hydrocarbyl and R105 is a C1-18 hydrocarbyl, said R¹⁰⁵ group forming a cyclic structure with Z, said hydrocarbyl group Q being according to Formula 1 d:

Formula 1 d

In an embodiment, said hydrocarbyl group Q can be an α-olefin according to Formula 1 c or an unsaturated cyclic hydrocarbyl group according to Formula 1 d. Preferably, hydrocarbyl group Q is an α-olefin or an unsaturated cyclic hydrocarbyl group.

Z is a branched or unbranched hydrocarbyl spacer group consisting of between 1 and 18 carbon atoms, preferably 2 and 8 carbon atoms, more preferably 4 and 7 carbon atoms, even more preferably 5 or 6 carbon atoms. Z is optionally substituted with hydrogen, carbon, and heteroatoms.

In an embodiment, hydrocarbyl group Q is an α-olefin according to Formula 1 c. Said a-olefin has up to and including 30 carbon atoms, such as up to and including 20 carbon atoms, preferably up to and including 10 carbon atoms, such as ethenyl, propenyl, butenyl, heptenyl, hexenyl, septenyl, octenyl, nonenyl or decenyl and can be unbranched or branched.

In a preferred embodiment, said α-olefin is an unbranched α-olefin according to Formula 1 e. In other words, the aluminum hydrocarbyl functionality comprises at least one hydrocarbyl chain bearing an α-olefin (i.e. hydrocarbyl group Q). Said hydrocarbyl group Q is an a-olefin-comprising a main group metal.

Formula 1 e In a preferred embodiment, hydrocarbyl group Q is an a-olefin according to Formula 1 e where n is 1 -5. In other words, the hydrocarbyl group Q is 3-buten-1-yl, 4-penten-1 -yl, 5- hexen-1-yl, 6-hepten-1-yl or 7-octen-1 yl.

In an embodiment, the hydrocarbyl group Q is an unsaturated cyclic hydrocarbyl group according to Formula 1 d. In said cyclic olefin the alkene is situated between substituents R¹⁰⁵ and Z and R¹⁰⁵ forms at least one ring with Z. R¹⁰⁵ can be a C1 -C18 hydrocarbyl, which forms one or more bonds with Z to form a cyclic group.

The number of R groups around the main group metal is dependent on the oxidization state of the metal. For example, when the main group metal is zinc or magnesium or calcium, the oxidation state is +2, and the formula is R¹⁰⁰MR¹⁰¹. For example, when the main group metal is aluminum or boron or gallium, the oxidation state is +3, and the formula is R¹⁰⁰R¹⁰¹ MR¹⁰².

In a preferred embodiment, at least one olefin comprising a main group metal hydrocarbyl functionality can be for example ethyl(7-octen 1 -yl) zinc or bis(7-octen-1 - yl) zinc.

In a preferred embodiment, an olefin comprising at least one main group metal hydrocarbyl functionality can for example be selected from one or more from the group of: di(isobutyl)(7- octen-1-yl) aluminum, di(isobutyl)(5-hexen-1-yl) aluminum, di(isobutyl)(3-buten-1-yl) aluminum, aluminum, tris(7-octen-1-yl) aluminum, tris(5-hexen-1 -yl) aluminum and/or tris(3- buten-1-yl) aluminum.

In an embodiment, the copolymerization of at least one olefin comprising main group metal hydrocarbyl chain transfer agent functionality and another α-olefin monomer may also for example be carried out in the presence of an additional chain transfer agent or chain shuttling agent. As non-limiting examples of chain transfer and/or chain shuttling agents main group metal hydrocarbyl or hydride chain transfer agents such as for example the following be used: one or more hydrocarbyl or hydride groups attached to a main group metal selected from aluminum, magnesium, calcium, zinc, gallium or boron.

Catalyst system suitable for use in step A)

A catalyst system for use in step a) comprises at least two of the following components:

i) a metal catalyst or metal catalyst precursor comprising a metal from Group 3-10 of the l UPAC 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 fun ctionality of the second type of olefin monomer; and optionally at least one or more of

ii) a co-catalyst

iii) a scavenger

Moreover, an additional main group metal hydrocarbyl chain transfer agent or a main group metal hydrocarbyl chain shuttling agent can be added as additional chain transfer agents and/or chain shuttling agents to insure reversible chain transfer polymerization.

The chain transfer agent functionality can also be a chain shuttling agent functionality.

In an embodiment, the catalyst system used in step A) further comprises an additional main group metal hydrocarbyl chain transfer agent or main group metal hydrocarbyl chain shuttling agent, selected from the group consisting of hydrocarbyl aluminum, hydrocarbyl magnesium, hydrocarbyl zinc, hydrocarbyl gallium, hydrocarbyl boron, hydrocarbyl calcium, aluminum hydride, magnesium hydride, zinc hydride, gallium hydride, boron hydride, calcium hydride and a combination thereof. An additional main group metal hydrocarbyl chain transfer agent can also be a chain shuttling agent.

The comonomer, which can also act as chain transfer agent, may be present in a molar ratio of between 10:1 to 10000:1 , preferred 20:1 to 2000:1 , further preferred between 100:1 to 500:1 , compared to the catalyst. The chain shuttling agent may be present in a molar ratio of between 1 :1 to 1000:1 , preferred 5:1 to 300:1 , further preferred between 10:1 to 100:1 , compared to the catalyst.

Chain shuttling agent as used in the present description means: a compound that is capable of reversibly interchanging hydrocarbyls with catalysts or other chain transfer agents. It is a metal compound comprising at least one ligand with a weak chemical bond. A chain shuttling agent can thus be a chain transfer agent.

Suitable catalysts and/or catalyst precursors are discussed in this section as well as suitable co-catalysts and scavengers, which are optional.

A catalyst for step A) can be used without co-catalyst, a catalyst precursor for step A) requires a co-catalyst to obtain the actual active catalyst. In the present invention, the catalyst may thereby preferably be selected so that it might undergo chain transfer polymerization with the main group metal hydrocarbyl functionality of the second type of olefin monomer.

The catalyst may lead to chain transfer with a chain transfer agent, such as for example hydrogen or silanes.

One or more scavenger that can be used for example to scavenge impurities from the reaction medium prior and during the polymerization process, can be selected for example from the group consisting of: trialkyl aluminum, especially for example triisobutyl aluminum, MAO, DMAO, MMAO, SMAO.

Metal catalyst and/or catalyst precursor suitable for step A)

In the section below several examples for metal catalysts or metal catalyst precursors, which may be used to prepare the metal catalyst according to the present invention, are specified. Metal catalysts that are suitable for use in step A) of the present invention may be obtained by reacting the metal catalyst precursors with a co-catalyst either prior to use in step A) or by in situ reaction with a co-catalyst. According to the present invention, the metal catalyst has a metal center selected from a Group 3 metal, a Group 4 metal, a Group 5 metal, a Group 6 metal, a Group 7 metal, a Group 8 metal, a Group 9 metal or a Group 10 metal, preferably Y, Ti, Zr, Hf, V, Cr, Fe, Co, Ni, Pd.

Ziegler-Natta catalysts as reported in US2009/0048399, US2014/0350200, W096/32427, WO01/23441 , WO2007/134851 , US4978648, EP1283 222A1 , US5556820; US4414132; US5106806 and US5077357 may also be suitable to use as metal catalyst precursors in the present invention.

The metal catalysts or metal catalyst precursors may for example be a C₃-, C or C2- symmetric zirconium or hafnium metallocene, preferably an indenyl substituted zirconium or hafnium dihalide, more preferably a bridged bis-indenyl zirconium or hafnium dihalide, even more preferably rac-dimethylsilyl bis-indenyl zirconium or hafnium dichloride (rac- Me2Si(lnd)2ZrC and rac-Me2Si(lnd)2HfCb, respectively), or rac-dimethylsilyl bis-(2-methyl- 4-phenyl-indenyl) zirconium or hafnium dichloride (rac-Me2Si(2-Me-4-Ph-lnd)2ZrCl2 and rac-Me₂Si(2-Me-4-Ph-lnd)2HfCl2, respectively).

According to the invention, said catalyst precursor can be for example a so-called half- metallocene, or constrained geometry catalyst, even more preferably, C₅Me₅[(C6Hi

[Me₂Si(C₅Me₄)N(tBu)]TiCl2, [C₅Me₄(CH₂CH₂N Me2]TiCl2. According to the invention, said catalyst can be for example a so-called post- metallocene, preferably [Et₂NC(N(2,6-iPr2-C6H₃)]TiCl3 or [N-(2,6-di(l- methylethyl)phenyl)amido)(2-isopropylphenyl)(a-naphthalen-2-diyl(6-pyridin-2- diyl)methane)]hafnium dimethyl.

The metal catalyst or metal catalyst precursor can also be for example a preferably C_s or Ci symmetric compound according to the formula (C5 ⁸ ₄) ⁹(Ci3 ⁸8)ML¹ _n, where C5 ⁸ ₄ is an unsubstituted or substituted cyclopentadienyl, and C i3R¹¹s is an unsubstituted fluorenyl group or a substituted fluorenyl group; and the bridging R⁹ group is selected from the group consisting of -Si(Me)2-, -Si(Ph)2-, -C(Me)2- or - C(Ph)2-, thus producing Ci- and Cs-symmetric metallocenes. Non-limiting examples of zirconocene dichloride metal catalyst precursors suitable for use in the present invention include: bis(cyclopentadienyl) zirconium dichloride, bis(methyl-cyclopentadienyl) zirconium dichloride, bis(n-propyl-cyclopentadienyl) zirconium dichloride, bis(n-butyl-cyclopentadienyl) zirconium dichloride, bis(1 ,3- dimethyl-cyclopentadienyl) zirconium dichloride, bis(1 ,3-di-t-butyl-cyclopentadienyl) zirconium dichloride, bis(1 ,3-ditrimethylsilyl-cyclopentadienyl) zirconium dichloride, bis(1 ,2,4-trimethyl-cyclopentadienyl) zirconium dichloride, bis(1 ,2,3,4-tetramethyl- cyclopentadienyl) zirconium dichloride, bis(pentamethylcyclopentadienyl) zirconium dichloride, bis(indenyl) zirconium dichloride, bis(2-phenyl-indenyl) zirconium dichloride, bis(fluorenyl) zirconium dichloride, bis(tetrahydrofluorenyl) zirconium dichloride, dimethylsilyl-bis(cyclopentadienyl) zirconium dichloride, dimethylsilyl-bis(3- t-butyl-cyclopentadienyl) zirconium dichloride, dimethylsilyl-bis(3-trimethylsilyl- cyclopentadienyl) zirconium dichloride, dimethylsilyl-bis(tetrahydrofluorenyl) zirconium dichloride, dimethylsilyl-(1 -indenyl)(cyclopentadienyl) zirconium dichloride, dimethylsilyl-(1 -indenyl)(fluorenyl) zirconium dichloride, dimethylsilyl-(1 - indenyl)(octahydrofluorenyl) zirconium dichloride, rac-dimethylsilyl-bis(2-methyl-3-t- butyl-cyclopentadienyl) zirconium dichloride, rac-dimethylsilyl-bis(l -indenyl) zirconium dichloride, rac-dimethylsilyl-bis(4,5,6,7-tetrahydro-1 -indenyl) zirconium dichloride, rac-dimethylsilyl-bis(2-methyl-1 -indenyl) zirconium dichloride, rac- dimethylsilyl-bis(4-phenyl-1 -indenyl) zirconium dichloride, rac-dimethylsilyl-bis(2- methyl-4-phenyl-1 -indenyl) zirconium dichloride, rac-ethylene-bis(l -indenyl) zirconium dichloride, rac-ethylene-bis(4,5,6,7-tetrahydro-1 -indenyl) zirconium dichloride, rac-1 , 1 ,2,2-tetramethylsilanylene-bis(1 -indenyl) zirconium dichloride, rac- 1 , 1 ,2,2-tetramethylsilanylene-bis(4,5,6,7-tetrahydro-1 -indenyl) zirconium dichloride, rac-ethylidene(1 -indenyl)(2,3,4,5-tetramethyl-1 -cyclopentadienyl) zirconium dichloride, rac-[1 -(9-fluorenyl)-2-(2-methylbenzo[b]indeno[4,5-d]thiophen-1 - yl)ethane]zirconium dichloride, dimethylsilyl bis(cyclopenta-phenanthren-3-ylidene) zirconium dichloride, dimethylsilyl bis(cyclopenta-phenanthren-l -ylidene) zirconium dichloride, dimethylsilyl bis(2-methyl-cyclopenta-phenanthren-1 -ylidene) zirconium dichloride, dimethylsilyl bis(2-methyl-3-benz-inden-3-ylidene) zirconium dichloride, dimethylsilyl-bis[(3a, 4,5,6, 6a)-2,5-dimethyl-3-(2-methylphenyl)-6H-cyclopentathien-6- ylidene] zirconium dichloride, dimethylsilyl-(2,5-dimethyl-1 -phenylcyclopenta[b]pyrrol- 4(1 H)-ylidene)(2-methyl-4-phenyl-1 -indenyl) zirconium dichloride, bis(2-methyl-1 - cyclopenta-phenanthren-1 -yl)zirconium dichloride, [ortho-bis(4-phenyl-2-indenyl) benzene] zirconium dichloride, [ortho-bis(5-phenyl-2-indenyl) benzene] zirconium dichloride, [ortho-bis(2-indenyl)benzene] zirconium dichloride, [ortho-bis (1 -methyl-2- indenyl)benzene] zirconium dichloride, [2,2'-(1 ,2-phenyldiyl)-1 ,1'dimethylsilyl- bis(indenyl)] zirconium dichloride, [2,2'-(1 ,2-phenyldiyl)-1 , 1 '-(1 ,2-ethanediyl)- bis(indenyl)] zirconium dichloride, dimethylsilyl-(cyclopentadienyl)(9-fluorenyl) zirconium dichloride, diphenylsilyl-(cyclopentadienyl)(fluorenyl) zirconium dichloride, dimethylmethylene-(cyclopentadienyl)(fluorenyl) zirconium dichloride, diphenylmethylene-(cyclopentadienyl)(fluorenyl) zirconium dichloride, dimethylmethylene-(cyclopentadienyl)(octahydrofluorenyl) zirconium dichloride, diphenylmethylene-(cyclopentadienyl)(octahydrofluorenyl) zirconium dichloride, dimethylmethylene-(cyclopentadienyl)(2,7-di-t-butyl-fluorenyl) zirconium dichloride, diphenylmethylene-(cyclopentadienyl)(2,7-di-t-butyl-fluorenyl) zirconium dichloride, dimethylmethylene-(3-methyl-1 -cyclopentadienyl)(fluorenyl) zirconium dichloride, diphenylmethylene-(3-methyl-1 -cyclopentadienyl)(fluorenyl) zirconium dichloride, dimethylmethylene-(3-cyclohexyl-1 -cyclopentadienyl)(fluorenyl) zirconium dichloride, diphenylmethylene-(3-cyclohexyl-1 -cyclopentadienyl)(fluorenyl) zirconium dichloride, dimethylmethylene-(3-t-butyl-1 -cyclopentadienyl)(fluorenyl) zirconium dichloride, diphenylmethylene-(3-t-butyl-1 -cyclopentadienyl)(fluorenyl) zirconium dichloride, dimethylmethylene-(3-ademantyl-1 -cyclopentadienyl)(fluorenyl) zirconium dichloride, diphenylmethylene-(3-ademantyl-1 -cyclopentadienyl)(fluorenyl) zirconium dichloride, dimethylmethylene-(3-methyl-1 -cyclopentadienyl)(2,7-di-t-butyl-fluorenyl) zirconium dichloride, diphenylmethylene-(3-methyl-1 -cyclopentadienyl)(2,7-di-t-butyl-fluorenyl) zirconium dichloride, dimethylmethylene-(3-cyclohexyl-1 -cyclopentadienyl)(2,7-di-t- butyl-fluorenyl) zirconium dichloride, diphenylmethylene-(3-cyclohexyl-1 - cyclopentadienyl)(2,7-di-t-butyl-fluorenyl) zirconium dichloride, dimethylmethylene-(3- t-butyl-1 -cyclopentadienyl)(2,7-di-t-butyl-fluorenyl) zirconium dichloride, diphenylmethylene-(3-t-butyl-1 -cyclopentadienyl)(2,7-di-t-butyl-fluorenyl) zirconium dichloride, dimethylmethylene-(3-methyl-cyclopentadienyl)(octahydro-octamethyl- dibenzo-fluorenyl) zirconium dichloride, diphenylmethylene-(3-methyl- cyclopentadienyl)(octahydro-octamethyl-dibenzo-fluorenyl) zirconium dichloride, dimethylmethylene-(3-cyclohexyl-cyclopentadienyl)(octahydro-octamethyl-dibenzo- fluorenyl) zirconium dichloride, diphenylmethylene-(3-cyclohexyl- cyclopentadienyl)(octahydro-octamethyl-dibenzo-fluorenyl) zirconium dichloride, dimethylmethylene-(3-t-butyl-cyclopentadienyl)(octahydro-octamethyl-dibenzo- fluorenyl) zirconium dichloride, diphenylmethylene-(3-t-butyl- cyclopentadienyl)(octahydro-octamethyl-dibenzo-fluorenyl) zirconium dichloride, dimethylmethylene-(3-ademantyl-cyclopentadienyl)(octahydro-octamethyl-dibenzo- fluorenyl) zirconium dichloride, diphenylmethylene-(3-ademantyl- cyclopentadienyl)(octahydro-octamethyl-dibenzo-fluorenyl) zirconium dichloride.

In a preferred embodiment, the metal catalyst or metal catalyst precursor can be for example: [[2,2'-[[[2-(dimethylamino-KN)ethyl]imino-KN]bis(methylene)]bis[4,6-bis(1 , 1 - dimethylethyl) phenolato-κθ]] zirconium dibenzyl, (phenylmethyl)[[2,2'-[(propylimino- KN)bis(methylene)]bis[4,6-bis(1 , 1 -dimethylethyl)phenolato-KO]] zirconium dibenzyl or (phenylmethyl)[[2,2'-[[[(2-pyridinyl-KN)methyl]imino-KN]bis(methylene)]bis[4,6-bis(1 , 1 - dimethylethyl)phenolato-KO]] zirconium dibenzyl.

In a preferred embodiment, complexes as reported in WO 00/43426, WO 2004/081064, US 2014/0039138 Al, US 2014/0039139 Al and US 2014/0039140 Al are suitable to use as metal catalyst precursors for the processes of the prese nt invention.

Compounds analogous to those listed above but where Zr has been replaced by Hf, so called hafnocenes, may also be used according to the as catalyst precursors present invention. The metal catalysts or metal catalyst precursors for use in the present invention may also be from post-metallocene catalysts or catalyst precursors.

In a preferred embodiment, the metal catalyst or metal catalyst precursor may be : [HN(CH2CH2N-2,4,6-Me3-C6H2)2]Hf(CH2Ph)2 or bis[N,N'-(2,4,6- trimethylphenyl)amido)ethylenediamine]hafnium dibenzyl. In a another preferred embodiment, the metal catalyst or metal catalyst precursor may be 2,6-diisopropylphenyl-N-(2-methyl-3-(octylimino)butan-2) hafnium trimethyl, 2,4,6- trimethylphenyl-N-(2-methyl-3-(octylimino)butan-2) hafnium trimethyl. In a preferred embodiment, the metal catalyst or metal catalyst precursor may be [2,6- iPr2C6H3NC(2-iPr-C6H4)-2-(6-C5H6)]HfMe2 — [N-(2,6-di(1 - methylethyl)phenyl)amido)(2-isopropylphenyl) (D-naphthalen-2-diyl(6-pyridin-2- diyl)methane)]hafnium dimethyl. Other non-limiting examples of metal catalyst precursors according to the present invention are: [N-(2,6-di(1 -methylethyl)phenyl)amido)(o-tolyl)(a-naphthalen-2-diyl(6- pyridin-2-diyl)methane)] hafnium dimethyl, [N-(2,6-di(1 -methylethyl)phenyl)amido)(o- tolyl)(a,a-naphthalen-2-diyl(6-pyridin-2-diyl)methane)] hafnium di(N, N- dimethylamido), [N-(2,6-di(l-methylethyl)phenyl)amido)(o-tolyl)(a,a-naphthalen-2- diyl(6-pyridin-2-diyl)methane)] hafnium dichloride, [N-(2,6-di( 1 - methylethyl)phenyl)amido)(phenanthren-5-yl)(a,a-naphthalen-2-diyl (6-pyridin-2- diyl)methane)] hafnium dimethyl, [N-(2,6-di( 1 - methylethyl)phenyl)amido)(phenanthren-5-yl)(a-naphthalen-2-diyl(6-pyridin 2- diyl)methane)] hafnium di(N,N-dimethylamido), [N-(2,6-di(l- methylethyl)phenyl)amido)(phenanthren-5-yl) (a-naphthalen-2-diyl(6-pyridin-2- diyl)methane)] hafnium dichloride. Other non-limiting examples include the family of pyridyl diamide metal dichloride complexes such as: [N-[2,6-bis( 1 -methylethyl)phenyl]- 6-[2-[phenyl(phenylamino-KN)methyl]phenyl]-2-pyridinemethanaminato(2-)- KN 1 , KN2]hafnium dichloride, [N-[2,6-bis( 1 -methylethyl)phenyl]-6-[2-[(phenylamino- KN)methyl]- 1 -naphthalenyl]-2-pyridinemethanaminato(2-)-KN 1 , KN2] hafnium dichloride, [N-[2,6-bis(1 -methylethyl)phenyl]-a-[2-( 1 -methylethyl)phenyl]-6-[2- [(phenylamino-KN)methyl]phenyl]-2-pyridinemethanaminato(2-)-KN 1 , KN2] hafnium dichloride, [N-(2,6-diethylphenyl)-6-[2-[phenyl(phenylamino-KN)methyl]- 1 - naphthalenyl]-2-pyridinemethanaminato(2-)-KN 1 , KN2]zirconium dichloride, [4-methyl- 2-[[2-phenyl- 1 -(2-pyridinyl-KN)ethyl]amino-KN]phenolato(2-)-

KO]bis(phenylmethyl)hafnium bis(phenylmethyl), [2-(1 , 1 -dimethylethyl)-4-methyl-6- [[2-phenyl-1 -(2-pyridinyl-KN)ethyl]amino-KN]phenolato(2-)-KO] hafnium bis(phenylmethyl), [2-(1 , 1 -dimethylethyl)-4-methyl-6-[[phenyl(2-pyridinyl-

KN)methyl]amino-KN]phenolato(2-)-KO]hafnium bis(phenylmethyl).

Non-limiting examples of titanium dichloride metal catalyst precursors suitable for use in the present invention include: cyclopentadienyl(P,P,P-tri-t-butylphosphine imidato) titanium dichloride, pentafluorophenylcyclopentadienyl(P,P, P-tri-t-butylphosphine imidato) titanium dichloride, pentamethylcyclopentadienyl(P,P, P-tri-t-butylphosphine imidato) titanium dichloride, 1 ,2,3,4-tetraphenyl-cyclopentadienyl(P,P,P-tri-t- butylphosphine imidato) titanium dichloride, cyclopentadienyl(P,P,P- tricyclohexylphosphine imidato) titanium dichloride, pentafluorophenyl cyclopentadienyl(P,P,P-tricyclohexylphosphine imidato) titanium dichloride, pentamethylcyclopentadienyl(P,P,P-tricyclohexylphosphine imidato) titanium dichloride, 1 ,2,3,4-tetraphenyl-cyclopentadienyl(P, P,P-tricyclohexylphosphine imidato) titanium dichloride, pentamethylcyclopentadienyl(P,P-dicyclohexyl-P- (phenylmethyl)phosphine imidato) titanium dichloride, cyclopentadienyl(2,6-di-t-butyl- 4-methylphenoxy) titanium dichloride, pentafluorophenylcyclopentadienyl(2,6-di-t- butyl-4-methylphenoxy) titanium dichloride, pentamethylcyclopentadienyl(2,6-di-t- butyl-4-methylphenoxy) titanium dichloride, 1 ,2,3-trimethyl-cyclopentadienyl(2,6- bis(l -methylethyl)phenolato) titanium dichloride, [(3a, 4,5,6, 6a-r))-2, 3, 4,5,6- pentamethyl-3aH-cyclopenta[b]thien-3a-yl](2,6-bis(1 -methylethyl)phenolato) titanium dichloride, pentamethylcyclopentadienyl(N,N'-bis(1 -methylethyl)ethanimidamidato) titanium dichloride, pentamethylcyclopentadienyl(N, N'- dicyclohexylbenzenecarboximidamidato) titanium dichloride, pentamethylcyclopentadienyl(N, N'-bis(1 -methylethyl)benzenecarboximidamidato) titanium dichloride, cyclopentadienyl(1 ,3-bis(1 , 1 -dimethylethyl)-2-imidazolidiniminato) titanium dichloride, cyclopentadienyl(1 ,3-dicyclohexyl-2-imidazolidiniminato) titanium dichloride, cyclopentadienyl(1 ,3-bis[2,6-bis(1 -methylethyl)phenyl]-2- imidazolidiniminato) titanium dichloride, pentafluorophenylcyclopentadienyl(1 ,3- bis(1 , 1 -dimethylethyl)-2-imidazolidiniminato) titanium dichloride, pentafluorophenylcyclopentadienyl(1 ,3-dicyclohexyl-2-imidazolidiniminato) titanium dichloride, pentafluorophenylcyclopentadienyl(1 ,3-bis[2,6-bis(1 -methylethyl)phenyl]- 2-imidazolidiniminato) titanium dichloride, pentamethylcyclopentadienyl(di-t- butylketimino) titanium dichloride, pentamethylcyclopentadienyl(2,2,4,4-tetramethyl-3- pentaniminato) titanium dichloride, [(3a, 4,5,6, 6a-r))-2, 4,5, 6-tetramethyl-3aH- cyclopenta[b]thien-3a-yl](2,2,4,4-tetramethyl-3-pentaniminato) titanium dichloride, cyclopentadienyl(N,N-bis(1 -methylethyl)benzenecarboximidamidato) titanium dichloride, pentafluorophenylcyclopentadienyl(N,N-bis(1 - methylethyl)benzenecarboximidamidato) titanium dichloride, pentamethylcyclopentadienyl(N, N-bis(1 -methylethyl)benzenecarboximidamidato) titanium dichloride, cyclopentadienyl(2,6-difluoro-N, N-bis(1 - methylethyl)benzenecarboximidamidato) titanium dichloride, pentafluorophenylcyclopentadienyl(2,6-difluoro-N,N-bis(1 - methylethyl)benzenecarboximidamidato) titanium dichloride, pentamethylcyclopentadienyl(2,6-difluoro-N,N-bis(1 - methylethyl)benzenecarboximidamidato) titanium dichloride, cyclopentadienyl(N,N - dicyclohexyl-2,6-difluorobenzenecarboximidamidato) titanium dichloride, pentafluorophenylcyclopentadienyl(N, N-dicyclohexyl-2,6- difluorobenzenecarboximidamidato) titanium dichloride, pentamethylcyclopentadienyl(N, N-dicyclohexyl-2,6- difluorobenzenecarboximidamidato) titanium dichloride, cyclopentadienyl(N,N,N',N'- tetramethylguanidinato) titanium dichloride, pentafluorophenylcyclopentadienyl(N, N,N',N'-tetramethylguanidinato) titanium dichloride, pentamethylcyclopentadienyl(N,N,N',N'-tetramethylguanidinato) titanium dichloride, pentamethylcyclopentadienyl(1 -(imino)phenylmethyl)piperidinato) titanium dichloride, pentamethylcyclopentadienyl chromium dichloride tetrahydrofuran complex.

Non-limiting examples of titanium (IV) dichloride metal catalyst suitable for use in the present invention are: (N-t-butylamido)(dimethyl)(tetramethylcyclopentadienyl)silane titanium dichloride, (N phenylamido)(dimethyl)(tetramethylcyclopentadienyl) silane titanium dichloride, (N sec-butylamido)(dimethyl)(tetramethylcyclopentadienyl)silane titanium dichloride, (N sec-dodecylamido) (dimethyl)(fluorenyl)silane titanium dichloride, (3 phenylcyclopentadien-1 -yl) dimethyl(t-butylamido) silane titanium dichloride, (3 (pyrrol-l-yl)cyclopentadien-l -yl) dimethyl(t-butylamido)silane titanium dichloride, (3,4-diphenylcyclopentadien-1 -yl)dimethyl(t-butylamido) silane titanium dichloride, 3 (3-N,N-dimethylamino)phenyl) cyclopentadien-1 -yl)dimethyl(t- butylamido) silane titanium dichloride, (P-t-butylphospho)(dimethyl) (tetramethylcyclopentadienyl) silane titanium dichloride. Other examples are the metal catalyst precursor cited in the list directly above wherein Ln is dimethyl, dibenzyl, diphenyl, 1 ,4-diphenyl-2-butene-1 ,4-diyl, 1 ,4-dimethyl-2-butene-1 ,4-diyl or 2,3- dimethyl-2-butene-1 ,4-diyl.

Suitable metal catalyst precursors can be also the trivalent transition metal as those described in WO 9319104 (for example see especially example 1 , page 13, line 15).

Suitable metal catalyst precursors can be also the trivalent transition metal as [C5Me4CH2CH2N(n-Bu)2]TiCI2 described in WO 9613529 (for example see especially example I I I , page 20, line 10-13) or [C5H(iPr)3CH2CH2N Me2]TiCI2 described in WO 97142232 and WO 9742236 (for example see especially example 1 , page 26, line 14).

In an embodiment, the metal catalyst precursor is [C5H4CH2CH2NMe2]TiCI2;

In an embodiment, the metal catalyst or metal catalyst precursor may also be [C5Me4CH2CH2NMe2]TiCI2, [C5H4CH2CH2NiPr2]TiCI2, [C5Me4CH2CH2NiPr2]TiCI2, [C5H4C9H6N]TiCI2, [C5H4CH2CH2NMe2]CrCI2, [C5Me4CH2CH2NMe2]CrCI2; [C5H4CH2CH2NiPr2]CrCI2, [C5Me4CH2CH2NiPr2]CrCI2 or [C5H4C9H6N]CrCI2.

A non-limiting list of examples of metal catalyst precursors that would be suitable according to the present invention are: (N, N dimethylamino)methyl- tetramethylcyclopentadienyl titanium dichloride, (N,N dimethylamino)ethyl- tetramethylcyclopentadienyl titanium dichloride, (N, N dimethylamino)propyl- tetramethylcyclopentadienyl titanium dichloride, (N,N dibutylamino)ethyl- tetramethylcyclopentadienyl titanium dichloride, (pyrrolidinyl)ethyl- tetramethylcyclopentadienyl titanium dichloride, (N,N-dimethylamino)ethyl-fluorenyl titanium dichloride, (bis(1 -methyl-ethyl)phosphino)ethyl-tetramethylcyclopentadienyl titanium dichloride, (bis(2-methyl-propyl)phosphino)ethyl-tetramethylcyclopentadienyl titanium dichloride, (diphenylphosphino)ethyl-tetramethylcyclopentadienyl titanium dichloride, (diphenylphosphino)methyldimethylsilyl-tetramethylcyclopentadienyl titanium dichloride. Other examples are the catalysts cited in the list directly above wherein Ln wherein the chloride can be replaced with bromide, hydride, methyl, benzyl, phenyl, allyl, (2-N, N-dimethylaminomethyl)phenyl, (2-N,N- dimethylamino)benzyl, 2,6-dimethoxyphenyl, pentafluorophenyl, and/or wherein the metal is trivalent titanium or trivalent chromium.

In a preferred embodiment, the catalyst precursor is: [2-(2,4,6-iPr3-C6H2)-6-(2,4,6- iPr3-C6H2)-C5H3N]Ti(CH2Ph)3 or [Et2NC(N-2,6-iPr2-C6H3)2]TiCI3

Other non-limiting examples of metal catalyst precursors according to the present invention are: {N',N"-bis[2,6-di(1 -methylethyl)phenyl]-N, N-diethylguanidinato} titanium trichloride, {N', N"bis[2,6-di(1 -methylethyl)phenyl]-N-methyl-N-cyclohexylguanidinato} titanium trichloride, {N',N"-bis[2,6-di(1 -methylethyl)phenyl]-N,N- pentamethyleneguanidinato} titanium trichloride, {N', N"-bis[2,6-di(methyl)phenyl]-sec- butyl-aminidinato} titanium trichloride, {N-trimethylsilyl,N'-(N",N"- dimethylaminomethyl)benzamidinato} titanium d ichloride TH F complex, {N- trimethylsilyl,N'-(N",N"-dimethylaminomethyl)benzamidinato} vanadium dichloride THF complex, {N,N'-bis(trimethylsilyl)benzamidinato} titanium dichloride THF complex, {N,N'-bis(trimethylsilyl)benzamidinato} vanadium dichloride THF complex. In a preferred embodiment, the catalyst precursor can be for example : [C5H3N{CMe=N(2,6-iPr2C6H3)}2]FeCI2, [2,4-(t-Bu)2,-6-(CH = NC6F5)C6H20]2TiCI2 or bis[2-(1 , 1 -dimethylethyl)-6-[(pentafluorophenylimino)methyl] phenolato] titanium dichloride. Other non-limiting examples of metal catalyst precursors according to the present invention can be for example: bis[2-[(2-pyridinylimino)methyl]phenolato] titanium dichloride, bis[2-(1 , 1 -dimethylethyl)-6-[(phenylimino)methyl]phenolato] titanium dichloride, bis[2-(1 , 1 -dimethylethyl)-6-[(1 - naphthalenylimino)methyl]phenolato] titanium dichloride, bis[3-

[(phenylimino)methyl][1 , 1 '-biphenyl]-2-phenolato] titanium dichloride, bis[2-(1 , 1 - dimethylethyl)-4-methoxy-6-[(phenylimino)methyl]phenolato] titanium dichloride, bis[2,4-bis(1 -methyl-1 -phenylethyl)-6-[(phenylimino)methyl]phenolato] titanium dichloride, bis[2,4-bis(1 , 1 -dimethylpropyl)-6-[(phenylimino)methyl]phenolato] titanium dichloride, bis[3-(1 , 1 -dimethylethyl)-5-[(phenylimino)methyl][1 , 1 '-biphenyl]-4- phenolato] titanium dichloride, bis[2-[(cyclohexylimino)methyl]-6-(1 , 1 - dimethylethyl)phenolato] titanium dichloride, bis[2-(1 , 1 -dimethylethyl)-6-[[[2-(1 - methylethyl)phenyl]imino]methyl]phenolato] titanium dichloride, bis[2-(1 , 1 - dimethylethyl)-6-[(pentafluorophenylimino)ethyl]phenolato] titanium dichloride, bis[2- (1 , 1 -dimethylethyl)-6-[(pentafluorophenylimino)propyl]phenolato] titanium dichloride, bis[2,4-bis(1 , 1 -dimethylethyl)-6-[1 -(phenylimino)ethyl]phenolato] titanium dichloride, bis[2,4-bis(1 , 1 -dimethylethyl)-6-[1 -(phenylimino)propyl]phenolato] titanium dichloride, bis[2,4-bis(1 , 1 -dimethylethyl)-6-[phenyl(phenylimino)methyl]phenolato] titanium dichloride. Other examples are the metal catalyst precursor cited in the list directly above wherein the dichloride can be replaced with dimethyl, dibenzyl, diphenyl, 1 ,4- diphenyl-2-butene-1 ,4-diyl, 1 ,4-dimethyl-2-butene-1 ,4-diyl or 2,3-dimethyl-2-butene- 1 ,4-diyl; and/or wherein the metal may be zirconium or hafnium.

In a preferred embodiment, the catalyst precursor can be : [2-[[[2-[[[3,5-bis(1 , 1 - dimethylethyl)-2-(hydroxy-KO)phenyl]methyl]amino-KN]ethyl]methylamino-KN]methyl]- 4,6-bis(1 , 1 -dimethylethyl)phenolato(2-)-KO] titanium bis(phenylmethyl), [2,4-dichloro- 6-[[[2-[[[3,5-dichloro-2-(hydroxy-KO)phenyl]methyl]amino-KN]ethyl]methylamino- KN]methyl]phenolato(2-)-KO] titanium bis(phenylmethyl), [2-[[[[1 -[[2-(hydroxy-KO)-3,5- diiodophenyl]methyl]-2-pyrrolidinyl-KN]methyl]amino-KN]methyl]-4-methyl-6- tricyclo[3.3.1 .13,7]dec-1 -ylphenolato(2-)-KO] titanium bis(phenylmethyl), [2-[[[2-[[[[2- (hydroxy-KO)-3,5-bis(1 -methyl-1 -phenylethyl)phenyl]methyl]methylamino- KN]methyl]phenyl]methylamino-KN]methyl]-4,6-bis(1 -methyl-1 - phenylethyl)phenolato(2-)-KO] titanium bis(phenylmethyl), [2,4-dichloro-6-[[[2-[[[[3,5- dichloro-2-(hydroxy-KO)phenyl]methyl]amino-KN]methyl]phenyl]amino- KN]methyl]phenolato(2-)-KO] titanium bis(phenylmethyl). Other examples are the metal catalyst precursor cited in the list directly above wherein bis(phenylmethyl) can be replaced with dichloride, dimethyl, diphenyl, 1 ,4-diphenyl-2-butene-1 ,4-diyl, 1 ,4- dimethyl-2-butene-1 ,4-diyl or 2,3-dimethyl-2-butene-1 ,4-diyl; and/or wherein the metal may be zirconium or hafnium. A non-limiting list of examples of chromium catalysts that would be suitable for use in to the present invention are:

(N-t-butylamido)(dimethyl)(tetramethylcyclopentadienyl)silane chromium bis(trimethylsilyl)methyl, (N-phenylamido)(dimethyl)(tetramethylcyclopentadienyl) silane chromium bis(trimethyl)methyl, (N-sec-butylamido)(dimethyl)

(tetramethylcyclopentadienyl)silane chromium bis(trimethylsilyl)methyl, (N-sec- dodecylamido)(dimethyl)(fluorenyl)silane chromium hydride triphenylphosphine, (P-t- butylphospho)(dimethyl)(tetramethylcyclopentadienyl) silane chromium bis(trimethylsilyl)methyl. Other examples are the catalysts cited in the list directly above wherein L1 is hydride, methyl, benzyl, phenyl, allyl, (2-N,N- dimethylaminomethyl)phenyl, (2-N,N-dimethylamino)benzyl; in other words chromium methyl, chromium benzyl, chromium allyl, chromium (2-N,N-dimethylamino)benzyl; and/or wherein the metal is trivalent yttrium or samarium; Other examples are metal catalyst precursors as cited in the list directly above wherein Ln is chloride, bromide, hydride, methyl, benzyl, phenyl, allyl, (2-N,N-dimethylaminomethyl)phenyl, (2-N,N- dimethylamino)benzyl and/or wherein the metal is trivalent titanium or trivalent chromium. Non-limiting examples of metal catalyst precursors according to the present invention are: N,N'-1 ,2-acenaphthylenediylidenebis(2,6-bis(1 -methylethyl)benzenamine) nickel dibromide, N,N'-1 ,2-ethanediylidenebis(2,6-dimethylbenzenamine) nickel dibromide, N,N'-1 ,2-ethanediylidenebis(2,6-bis(1 -methyl-ethyl)benzenamine) nickel dibromide, N,N'-1 ,2-acenaphthylenediylidenebis(2,6-dimethylbenzenamine) nickel dibromide, N,N'-1 ,2-acenaphthylenediylidenebis(2,6-bis(1 -methylethyl)benzenamine) nickel dibromide, N,N'-1 ,2-acenaphthylenediylidenebis(1 , 1 '-biphenyl)-2-amine nickel dibromide. Other examples are the catalysts cited in the list directly above wherein bromide can be replaced with chloride, hydride, methyl, benzyl and/or the metal can be palladium.

Further non-limiting examples of metal catalyst precursors according to the present invention are: [2-[[[2,6-bis(1 -methylethyl)phenyl]imino-KN]methyl]-6-(1 , 1 - dimethylethyl)phenolato-KO] nickel phenyl(triphenylphosphine), [2-[[[2,6-bis(1 - methylethyl)phenyl]imino-KN]methyl]-6-(1 , 1 -dimethylethyl)phenolato-KO] nickel phenyl(triphenylphosphine), [2-[[[2,6-bis(1 -methylethyl)phenyl]imino- KN]methyl]phenolato-KO] nickel phenyl(triphenylphosphine)-, [3-[[[2,6-bis(1 - methylethyl)phenyl]imino-KN]methyl][1 , 1 '-biphenyl]-2-olato-KO] nickel phenyl(triphenylphosphine)-, [2-[[[2,6-bis(1 -methylethyl)phenyl]imino-KN]methyl]-4- methoxyphenolato-κθ] nickel phenyl(triphenylphosphine), [2-[[[2,6-bis(1 - methylethyl)phenyl]imino-KN]methyl]-4-nitrophenolato-KO] nickel phenyl(triphenylphosphine), [2,4-diiodo-6-[[[3,3",5,5"- tetrakis(trifluoromethyl)[1 , 1 ':3', 1 "-terphenyl]-2'-yl]imino-KN]methyl]phenolato-KO] nickel methyl[[3,3',3"-(phosphinidyne-KP)tris[benzenesulfonato]]] trisodium; [2,4- diiodo-6-[[[3_!3 5_!5"-tetrakis(trifluoromethyl)[1 _! 1 ':3'_! 1 "-terphenyl]-2'-yl]imino- KN]methyl]phenolato-KO] nickel methyl[[3,3'-(phenylphosphinidene-

KP)bis[benzenesulfonato]]]-disodium. Co-catalvst suitable for step A)

A co-catalyst can be used when a metal catalyst precursor is used. A co-catalyst may thereby be an alkylating agent and/or reducing agent and/or cationization agent for the catalyst precursor and/or a scavenger. The function of this co-catalyst is to activate the metal catalyst precursor. Co-catalyst may be selected for example from aluminum alkyls and aluminum alkyl halides, such as for example triethyl aluminum (TEA) or diethyl aluminum chloride (DEAC). Co-catalysts may be selected for example from the group consisting of MAO, DMAO, MMAO, SMAO, possibly in combination with aluminum alkyls, for example triisobutyl aluminum, and/or with a combination of an aluminum alkyl, for example triisobutyl aluminum, and a fluorinated aryl borane or fluorinated aryl borate (viz. B(R')_y wherein R' is a fluorinated aryl and y is 3 or 4, respectively). Examples of a fluorinated borane is B(CeF₅)3 and of fluorinated borates are [X]⁺[B(C₆F₅)₄]- (e.g. X = Ph₃C, C₆H₅N(H)Me2).

Methylaluminoxane or MAO as used in the present description may mean: a compound derived from the partial hydrolysis of trimethyl aluminum that serves as a co-catalyst for catalytic olefin polymerization.

Supported methylaluminoxane or SMAO as used in the present description may mean: a methylaluminoxane bound to a solid support.

Depleted methylaluminoxane or DMAO as used in the present description may mean: a methylaluminoxane from which the free trimethyl aluminum has been removed. Modified methylaluminoxane or MMAO as used in the present description may mean: modified methylaluminoxane, viz. the product obtained after partial hydrolysis of trimethyl aluminum plus another trialkyl aluminum such as tri(isobutyl) aluminum or tri- n-octyl aluminum.

Fluorinated aryl borates or fluorinated aryl boranes as used in the present description may mean: a borate compound having three or four fluorinated (preferably perfluorinated) aryl ligands or a borane compound having three fluorinated (preferably perfluorinated) aryl ligands.

For example, the co-catalyst can be an organometallic compound. The metal of the organometallic compound can be selected from Group 1 , 2, 12 or 13 of the lU PAC Periodic Table of Elements. Preferably, the co-catalyst is an organoaluminum compound, more preferably an aluminoxane, said aluminoxane being generated by the reaction of a trialkyl aluminum compound with water to partially hydrolyze said aluminoxane. For example, trimethyl aluminum can react with water (partial hydrolysis) to form methylaluminoxane (MAO). MAO has the general formula (AI(CH 3)3- nOo.5n)x- (AI Me3)y having an aluminum oxide framework with methyl groups on the aluminum atoms.

MAO generally contains significant quantities of free trimethyl aluminum (TMA), which can be removed by drying the MAO to afford the so-called depleted MAO or DMAO. Supported MAO (SMAO) may also be used and may be generated by the treatment of an inorganic support material, typically silica, by MAO. Alternatively to drying the MAO, when it is desired to remove the free trimethyl aluminum, a bulky phenol such as butylhydroxytoluene (BHT, 2,6-di-t-butyl-4- methylphenol) can be added which reacts with the free trimethyl aluminum.

Neutral Lewis acid modified polymeric or oligomeric aluminoxanes may also be used, such as alkylaluminoxanes modified by addition of a C1 -30 hydrocarbyl substituted Group 13 compound, especially a tri(hydrocarbyl) aluminum- or tri(hydrocarbyl) boron compounds, or a halogenated (including perhalogenated) derivatives thereof, having 1 to 10 carbons in each hydrocarbyl or halogenated hydrocarbyl group, more especially a trialkyl aluminum compound.

Other examples of polymeric or oligomeric aluminoxanes are tri(isobutyl) aluminum- or tri(n-octyl) aluminum-modified methylaluminoxane, generally referred to as modified methylaluminoxane, or MMAO. In the present invention, MAO, DMAO, SMAO and MMAO may all be used as co-catalyst.

In addition, for certain embodiments, the metal catalyst precursors may also be rendered catalytically active by a combination of an alkylating agent and a cation forming agent which together form the co-catalyst, or only a cation forming agent in the case the catalyst precursor is already alkylated, as exemplified in T. J. Marks et al., Chem. Rev. 2000, (100), 1391 . Suitable alkylating agents are trialkyl aluminum compounds, preferably TI BA. Suitable cation forming agents for use herein include (i) neutral Lewis acids, such as C1 -30 hydrocarbyl substituted Group 13 compounds, preferably tri(hydrocarbyl)boron compounds and halogenated (including perhalogenated) derivatives thereof, having from 1 to 10 carbons in each hydrocarbyl or halogenated hydrocarbyl group, more preferably perfluorinated tri(aryl)boron compounds, and most preferably tris(pentafluorophenyl) borane, (ii) non polymeric, compatible, non-coordinating, ion forming compounds of the type [C] ⁺[A]^" where "C" is a cationic group such as ammonium, phosphonium, oxonium, carbonium, silylium or sulfonium groups and [A]^" is an anion, especially for example a borate.

Non-limiting examples of the anionic ["A"] are borate compounds such as C1 -30 hydrocarbyl substituted borate compounds, preferably tetra(hydrocarbyl)boron compounds and halogenated (including perhalogenated) derivatives thereof, having from 1 to 10 carbons in each hydrocarbyl or halogenated hydrocarbyl group, more preferably perfluorinated tetra(aryl)boron compounds, and most preferably tetrakis(pentafluorophenyl) borate.

A supported co-catalyst may also be used, for example using silica supported MAO (SMAO) as the co-catalyst. The support material can be an inorganic material. Suitable supports include solid and particulated high surface area, metal oxides, metalloid oxides, or mixtures thereof. Examples include: talc, silica, alumina, magnesia, titania, zirconia, tin oxide, aluminosilicates, borosilicates, clays, and mixtures thereof.

Preparation of a supported catalyst can be carried out using methods known in the art, for example i) a metal catalyst precursor can be reacted with supported MAO to produce a supported catalyst; ii) MAO can be reacted with a metal catalyst precursor and the resultant mixture can be added to silica to form the supported catalyst; iii) a metal catalyst precursor immobilized on a support can be reacted with soluble MAO. Copolymerization of an olefin and an olefin comprising a main group metal hydrocarbyl chain transfer agent functionality

Step A) is preferably carried out in an inert atmosphere.

Copolymerization of the olefins can for example be carried out in the gas phase below the melting point of the polymer. Copolymerization can also be carried out in the slurry phase below the melting point of the polymer. Moreover, copolymerization can be carried out in solution at temperatures above the melting point of the polymer product.

It is known to continuously polymerize one or more olefins, such as ethylene or propylene, in solution or in slurry, e.g. in a continuous (multi) CSTR or (multi) loop reactor, in the gas-phase in a reactor with a fluidized or mechanically stirred bed or in a combination of these different reactors, in the presence of a catalyst based on a compound of a transition metal belonging to Groups 3 to 10 of the Periodic Table of the Elements.

Slurry phase polymerizations are typically carried out at temperatures in the range 50- 125 °C and at pressures in the range 1 -50 bar.

The present invention may also be carried out in a solution polymerization process. Typically, in the solution process, the monomer and polymer are dissolved in an inert solvent. Although a single reactor can be used, multiple reactors provide a narrower residence time distribution and therefore a better control of molecular weight distribution.

In an embodiment, long chain branched polyolefins having one or multiple long chain branches can have a number average molecular weight (M_n) between 500 and 1 ,000,000 g/mol, preferably between 1 ,000 and 200,000 g/mol.

The polyolefins having one or multiple functionalized long chain branches according to the present invention preferably have a polydispersity index (£> or PDI) of between 1 .1 and 10.0, more preferably between 1 .1 and 5.0, more preferably between 1 .1 and 4.0, even more preferably between 1 .5 and 2.5.

According to the present invention, content of comonomer can represent for example at between 0.01 mol-% and 70 mol-%, preferably between 0.05 mol-% and 30 mol-%, preferably between 0.06 mol-% and 20 mol-%, preferably between 0.07 mol-% and 1 5 mol-%, preferably between 0.08 mol-% and 1 0 mol-%, preferably between 0.09 mol- % and 8 mol-%, preferably between 0.1 mol-% and 7 mol-%, further preferred between 0.5 mol-% and 5 mol-%, further preferred between 1 mol-% and 4 mol-%, further preferred between 2 mol-% and 3 mol-% and/or at least 0.001 mol-%, further preferred least 0.01 mol-%, preferably 0.1 mol-%, further preferred 0.5 mol-%, further preferred at least 1 mol-%, preferred at least 10 mol-%, further preferred at least 1 5 mol-%, further preferred at least 20 mol-%, further preferred at least 30 mol-%, further preferred at least 40 mol-%, further preferred at least 50 mol-%, further preferred at least 60 mol-% of the obtained polymers.

Step B) oxidation

A second step of the process according to the present invention can be step B) and relates to contacting the polyolefin obtained in step A) with at least one oxidizing agent or safe oxidizing agent to obtain to obtain a polyolefin having one or more pending oxidized functionalities.

As safe oxidizing agent in step B) the following may for example be used: CO, CO2, CS₂, COS, R²NCO, R²N CS, R²NCN R³, CH₂=C(R²)C(=0)OR³, CH₂=C(R²)(C=0)N(R³)R⁴, CH₂=C(R²)P(=0)(OR³)OR⁴, N₂0, R²CN, R²NC, epoxide, aziridine, cyclic anhydride, R³R⁴C=NR², carbodiimides, R²C(=0)R³, CIC(=0)OR² and S0₃, preferably N₂0, C0₂ and S0₃. In an embodiment, an oxidizing agent or safe oxidizing agent used in the present invention can be dried. A dried safe oxidizing agent according to the invention can thereby preferably comprise less than 100 ppm of water, preferably less than 50 ppm of water, further preferred less than 20 ppm of water, even more preferred less than 10 ppm of water, even more preferred less than 5 ppm of water, even more preferred less than 3 ppm of water. This can contribute to improve oxidation yield.

The oxidizing agent can be for example gaseous, whereby the oxidation step can optionally be carried out for example at a pressure between 0.01 and 80 bar, preferably between 1 and 20 bar, further preferred between 2 and 10 bar. In an embodiment, the oxidation step can be carried out for example at a temperature of between O C and 250°C.

In an embodiment, the oxidation step can be for example carried out for a time period of between 0.5 minutes and 150 minutes, more preferably between 1 minutes and 120 minutes, further preferred between 30 minutes and 60 minutes depending on the reaction temperature and the oxidizing agent.

Step C)

In step C) the polyolefin having one or more pending oxidized functionalities obtained in step B) is used to obtain a graft copolymer by transesterification of a preformed transesterifiable polymer, especially a preformed polyester and/or a preformed polycarbonate, and/or by ring-opening polymerization of cyclic monomers, especially cyclic esters (lactones) and/or cyclic carbonates. In step C) one or more side chains, especially polyester and/or polycarbonate side chains, may thus be formed on the polyolefin main chain, wherein as initiators the pending oxidized functionalities on the polyolefin main chain obtained in step B) can be used to obtain a graft copolymer. Thus, the product of step B) is subsequently used in step C) as a macro-initiator for the formation of graft copolymer.

Preformed transesterifiable polymer, especially preformed polyester and/or a preformed polycarbonate, in the sense of the present invention may thereby mean for example commercially available or otherwise prepared or obtained before and/or independently from at least one or preferably all of the steps A), B), C) and D) according to the invention.

Step C) can be carried out in a hydrocarbon solvent, especially for example heptane, octane, decaline or an aromatic hydrocarbon solvent like toluene or xylene, or in other organic solvents, like DMF or tetrachloroethane, or in the melt.

The steps A) to C) described above can preferably for example be performed in cascadelike process for example either in the same or in subsequent/connected reactors or vessels, preferably without additional intermediary and/or workup and/or drying and/or purification steps, even more preferred without any further additional ROP or transesterification step, even further preferred continuously. In a cascade-like process, the polymer preparation can be carried out preferably without a metal-substitution step, especially for example by hydrolysis. It should be noted that an extruder can also be considered as a reactor in the context of the present invention.

A polyolefin-based graft copolymer obtained according to the present invention may comprise a first long chain branched polyolefin block and one or more polymer side chains and may have a number average molecular weight (M_n) between 500 and 1 ,000,000 g/mol, preferably between 2,000 and 500,000 g/mol, preferably between 5,000 and 250,000 g/mol, further preferred between 1 0,000 a nd 1 00,000 g/mol and/or a polydispersity index (£>) of between 1 .1 and 1 0.0, preferably between 2.0 and 5.0, whereby said polyolefin block may further optionally have for example a branching number determined by N MR of 0.2 to 1 0, preferably 0.5 to 5, even m ore preferred 1 to 3 per 1 0000 carbon atoms or of 50 to 3500, preferred 1 00 to 1 000, further preferred 200 to 900 per 1 0000 carbon atoms.

A polyolefin-based graft copolymer according to the invention may further also have polymer side chain(s), whereby the polymer side chain comprise(s) 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. Moreover, the polymer side chain(s) may have a number average molecular weight (M_n) between 500 and 1 ,000,000 g/mol, preferably between 500 and 100,000 g/mol, preferably between 500 and 50,000 g/mol, further preferred between 500 and 25,000 g/mol, alternatively between 500 and 10,000 g/mol, alternatively between 500 and 5,000 g/mol.

The polyolefin-based graft copolymers comprising a first long chain branched polyolefin block and one or multiple polymer side chains prepared according to the present invention may for example be used to introduce polar properties to enhance the interfacial interactions in polyolefins blends with polar polymers, such as for example blends with at least one polyester and/or at least one polycarbonate. They may be used for example as compatibilizers to improve properties such as adhesion . They may be used to improve barrier properties (especially against oxygen) and/or mechanical properties, like improved dimensional stability and/or improved heat resistance and/or improved stiffness, especially for example for polyolefin films. They may be used as compatibilizer to polar polymers such as for example starch or for polyolefin-polar polymer blends, polyolefin-based composites with inorganic fillers, such as glass or talcum . They may be used in drug delivery devices or for nanoporous materials/membranes. They may moreover be used to improve adhesion to other materials, such as for example glass and/or inorganic filers, to improve surface properties, such as for example paintability and/or printability, anti-fogging, anti-static properties. They may furthermore be used to improve chemical resistance and/or acoustic properties for example by reduced squeaking and/or rattling and/or reduced weight.

Examples

The invention is further illustrated by the following non-limiting examples merely used to further explain certain embodiments of the present invention . General considerations

All manipulations were performed under an inert dry nitrogen atmosphere using either standard Schlenk or glove box techniques. Dry, oxygen free toluene was employed as solvent for all polymerizations. Catalysts rac-Me2Si(l nd)2ZrCl2, C5Me₄(SiMe2NtBu)TiCl2 and rac-Me2Si(l nd)2HfCl2 were purchased from mCAT GmbH , Konstanz, Germany. Methylaluminoxane (MAO, 30 wt.% solution in toluene) was purchased from Chemtura. Tri(isobutyl) aluminum (TI BA, 1 .0 M solution in hexanes), tetrachloroethane-d2, diisobutylaluminum hydride solution (1 .0 M solution in TH F) were purchased from Sigma Aldrich. Trityl tetrakis(pentafluorophenyl)borate was purchased from Acros Organics. ω-Pentadecalactone (PDL) (98%, Sigma-Aldrich) was dried over Cahb and distilled under reduced pressure. Toluene (Sigma-Aldrich) was dried using an MBraun-SPS-800 purification column system. N'-bis(salicylidene)-2,2-dimethyl-1 ,3- propanediamine (98%, Sigma-Aldrich) was used as provided. AI(CH3)3 purchased from Aldrich was used in 2 M solution in toluene.

Size exclusion chromatography (SEC).

The number average molecular weight (M_n) in g/mol and polydispersity index (PDI ) were determined by means of high temperature size exclusion chromatography (HT SEC) which was performed at 160 °C using a high speed GPC (Freeslate, Sunnyvale, USA). Detection : I R4 (PolymerChar, Valencia, Spain). Column set: three Polymer Laboratories 1 3 μηη PLgel Olexis, 300 ^χ 7.5 mm. 1 ,2,4-Trichlorobenzene (TCB) was used as eluent at a flow rate of 1 m L-min ^"1. TCB was freshly distilled prior to use. The molecular weight was calculated from HT SEC analysis with respect to narrow polyethylene standards (PSS, Mainz, Germany).

Synthesis of di(isobutyl)(oct-7-en-1 -yl)aluminum (DI BAO)

Di(isobutyl)(oct-7-en-1 -yl)aluminum (DI BAO) was synthesized by hydroalumination of excess 1 ,7-octadiene using di(isobutyl)aluminum hydride at 60 °C for 6 h in a 200 mL Schlenk flask equipped with a magnetic stirrer. The remaining reagents (for example 1 ,7-octadiene) after the hydroalumination reaction were removed by evacuation .

Typical procedure for synthesis of PE-graff-PPDL copolymers via ROP. Copolymerization reactions of ethylene/di(isobutyl)(oct-7-en-1 -yl)aluminum (DI BAO) were carried out in stainless steel Buchi reactors (300 ml_). Prior to the polymerization, the reactor was dried in vacuo at 40 °C and flushed with nitrogen. Solvent (toluene), MAO solution (30% w/w in toluene) were introduced into the reactor and stirred at 150 rpm for 20-30 min. A solution of di(isobutyl)(oct-7-en-1 -yl)aluminum (DI BAO) comonomer was introduced under nitrogen atmosphere as a second type of olefin monomer comprising a main group metal hydrocarbyl functionality followed by the addition of the predefined amount of diethyl zinc solution, used as chain shuttling agent. The mixture was stirred for 10 min and saturated with lower flow of ethylene. The reaction was started by the addition of the predefined amount 5 micro moles of the catalyst solution under an inert atmosphere. The reactor was then pressurized to the desired pressure (2 bars) with ethylene and the pressure was maintained constant during the polymerization time (30 min) at 40 °C. At the end of the reaction, the ethylene feed was stopped and the residual ethylene was vented off. Polymerization conditions for experiments 1 to 5 (Exp. 1 to 5) are listed below in Table 1 . ln-situ oxidation procedure using synthetic air (about 20 vol.% of oxygen and 80 vol.% of nitrogen): after releasing the residual ethylene pressure, synthetic air was injected through a gas injection tube and the suspension was maintained under constant synthetic air pressure at 60 °C for 2 h with rigorous stirring (600 rpm).

Table 1

Exp. Catalyst cocatalyst cocat.: com:Zn: cat cat

1 rac-Me₂Si(lnd)2ZrCl2 MAO 760 500:25:1

2 rac-Me₂Si(lnd)2ZrCl2 [Ph3C] 2.0 300:25:1

[B(C6F5)4

3 C₅Me₄(SiMe2NtBu)TiCl2 MAO 800 350:20:1

4 C₅Me₄(SiMe2NtBu)TiCl2 [Ph3C] 2.0 350:20:1

[B(C6F5)4

5 rac-Me2Si(lnd)₂l-lfCl2 MAO 1000 350:20:1

6 rac-Me2Si(lnd)₂l-lfCl2 [Ph3C] 2.0 350:20:1

[B(C6F5)4 For each of the experiments 1 to 5, after venting off the remaining synthetic air, the reactor was charged with PDL (1.15 g 4.8 mmol) in toluene (10 ml). Temperature was raised to 100 °C and the reactor was maintained under stirring at 600 rpm during 2 hours. The synthesized copolymer was cooled to room temperature and quenched using acidified methanol, isolated and dried in vacuum at room temperature for 18 h.

Typical polymerization procedure for the preparation of PCL via ROP of caprolactone. In a glovebox, caprolactone (500 mg), Al-salen catalyst (74 μηηοΙ) and an equimolar amount of benzyl alcohol (8 mg, 74 μηηοΙ) were placed in a small glass crimp cap vial. Dry toluene was added (1 mL) and the vial was capped. The reaction mixture was removed from the glovebox and put in a carrousel reactor at 100 °C. For all reactions, an aliquot of crude polymer was withdrawn at the end of the polymerization reaction and dissolved in CDC in order to determine the conversion of the monomers by ¹H NMR spectroscopy. The reaction was then stopped by quenching the crude product with acidic ethanol solution (5 mL) to precipitate the polymer. The polymers were dried at 40 °C for 24 h under reduced pressure.

Synthesis of Al-salen catalyst

N,N'-bis(salicylidene)-2,2-dimethyl-1 ,3-propanediamine (2.0 g, 5.7 mmol) was suspended in toluene (30 mL) under N2 flow. Subsequently, AI(CH3)3 (2 M solution in toluene, 2.85 mL, 5.7 mmol) was added via syringe and the mixture was stirred at room temperature. The thus obtained solution was concentrated to half the original volume and pale yellow needles of Al-salen catalyst were isolated with a yield of 90%.

Typical polymerization procedure for the preparation of PCL via ROP of caprolactone. In a glovebox, caprolactone (500 mg), Al-salen catalyst (74 μηηοΙ) and an equimolar amount of benzyl alcohol (8 mg, 74 μηηοΙ) were placed in a small glass crimp cap vial. Dry toluene was added (1 mL) and the vial was capped. The reaction mixture was removed from the glovebox and put in a carrousel reactor at 100 C. For all reactions, an aliquot of crude polymer was withdrawn at the end of the polymerization reaction and dissolved in CDCI3 in order to determine the conversion of the monomers by ¹H NMR spectroscopy. The reaction was then stopped by quenching the crude product with acidic ethanol solution (5 mL) to precipitate the polymer. The polymers were dried at 40 °C for 24 h under reduced pressure.

Typical procedure for synthesis of PE-graff-PCL copolymers via transesterification. The experiments 1 to 5 described above where repeated, however after venting off the remaining synthetic air, the reactor was charged with PCL (2.0 g, M„ = 25.6 kg/mol, D = 1.3, prepared with the Al-salen catalyst according to the method described above) in toluene (10 ml) instead of PDL (see above). Temperature was raised to 100 °C and the reactor was maintained under stirring at 600 rpm during 48 hours. The synthesized copolymer was cooled to room temperature and quenched using acidified methanol, isolated and dried in vacuum at room temperature for 18 h.

Claims

CLAI MS

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 1 a: R^{1 00}(_n-2) ¹⁰¹ Mⁿ⁺R¹⁰² using a catalyst system to obtain a polyolefin; wherein said catalyst system comprises a co-catalyst, a scavenger, a catalyst or catalyst precursor comprising a metal from Group 3-10 of the l UPAC 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

wherein further M is a main group metal; n is the oxidation state of M; R¹⁰⁰, R¹⁰¹ and R¹⁰² of Formula 1 a 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 R¹⁰⁰, R¹⁰¹ and R¹⁰² is a hydrocarbyl group Q, wherein hydrocarbyl group Q is according to Formula 1 b:

(Formula 1 b)

wherein Z is bonded to M and Z is a C1 -C18 hydrocarbyl group; R¹⁰⁵ optionally forms a cyclic group with Z; wherein R¹⁰³ and R¹⁰⁴ and R¹⁰⁵ are each independently selected from hydrogen or a hydrocarbyl group; and at least one of the steps of:

B) an oxidizing step comprising contacting said polyolefin obtained in step with at least one oxidizing agent to obtain a polyolefin having one or more pending oxidized functionalities; and/or C) using the polyolefin having one or more pending oxidized functionalities obtained in step B) to obtain a graft copolymer by transesterification of a preformed transesterifiable polymer and/or by ring-opening polymerization of cyclic monomers.

2. Process according to claim 1 , wherein said oxidizing agent used in step B) is an oxidizing agent according to Formula I :

Formula I

wherein a is 1 , b and c are each independently 0 or 1 and X, Y, Z¹ and Z² are independently selected from carbon, hydrocarbyl or heteroatom .

3. Process according to claim 1 or 2, wherein the oxidizing agent used in step B) is selected from the group consisting of, CO, C0₂, CS₂, COS, R²NCO, R²NCS, R²NCNR³, CH₂=C(R²)C(=0)OR³, CH₂=C(R₂)(C=0)N(R³)R⁴,

CH₂=C(R²)P(=0)(OR³)OR⁴, N₂0, R²CN, R²NC, epoxide, aziridine, cyclic anhydride, R³R4C=NR², R²C(=0)R³, CIC(=0)OR² and S0₃, preferably N₂0, C0₂ and S0₃.

4. Process according to any one of the preceding claims, wherein at least one of R¹⁰⁰, R¹⁰¹ and R¹⁰² is a hydrocarbyl group Q and the remaining groups of R¹⁰⁰, R¹⁰¹ and R¹⁰² are each a C1 -C4 hydrocarbyl group or wherein two groups of R¹⁰⁰, R¹⁰¹ and R¹⁰² are each a hydrocarbyl group Q and the remaining group of R¹⁰⁰, R¹⁰¹ and R¹⁰² is a C1 -C4 hydrocarbyl group or wherein all of R¹⁰⁰, R¹⁰¹ and R¹⁰² are a hydrocarbyl group Q.

5. Process according to any one of the preceding claims, wherein the hydrocarbyl group Q according to Formula 1 b attached to a main group metal is a linear a-olefin group or a cyclic unsaturated hydrocarbyl group, preferably but-3-en-1- yl, pent-4-en-1-yl, hex-5-en-1 -yl, hept-6-en-1-yl or oct-7-en-1 yl, 5- ethylenebicyclo[2.2.1 ]hept-2-ene or 5-propylenebicyclo[2.2.1 ]hept-2-ene.

6. Process according to any one of the preceding claims, wherein at least one type of olefin monomer comprises a main group metal hydrocarbyl functionality that is preferably 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. Process according to any one of the preceding claims, wherein the co- catalyst is selected from the group consisting of TEA, DEAC, MAO, DMAO, MMAO, SMAO, possibly in combination with aluminum alkyls, for example triisobutyl aluminum, and/or with a combination of an aluminum alkyl, for example triisobutyl aluminum, and a fluorinated aryl borane or fluorinated aryl borate.

8. Process according to any one of the preceding claims, wherein a metal catalyst or metal catalyst precursor used in step A) comprises a metal from Group 3-8 of the l UPAC Periodic Table of elements, more preferably from Group 3-6 and/or wherein the metal catalyst or metal catalyst precursor used in step A) comprises a metal selected from the group consisting of Ti, Zr, Hf, V, Cr, Fe, Co, Ni, Pd, preferably Ti, Zr or Hf.

9. Process according to claim 8, wherein said metal catalyst or catalyst precursor is a C₃-, C-i -, or C2- symmetric zirconium metallocene, preferably an indenyl substituted zirconium dihalide, more preferably a bridged bis-indenyl zirconium dihalide, even more preferably rac-dimethylsilyl bis-indenyl zirconium dichloride (rac- Me2Si(lnd)2ZrCl2) or rac-dimethylsilyl bis-(2-methyl-4-phenyl-indenyl) zirconium dichloride (rac-Me₂Si(2-Me-4Ph-lnd)2ZrCl2.

10. Process according to claim 8 or 9, wherein said metal catalyst or metal catalyst precursor is [Me₂Si(C₅Me4)N(tBu)]TiCl2, Me₂Si(2-Me-4-Ph-lnd)₂HfCl2,

[C5Me4CH2CH2N(n-Bu)2]TiCl2, bis(n-propyl-cyclopentadienyl)ZrCl2, bis(n-butyl- cyclopentadienyl)ZrCl2.

1 1 . Process according to any one of the preceding claims, 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. Process according to any one of the preceding claims, wherein an additional main group metal hydrocarbyl chain transfer agent used in step A) 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.

1 3. 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 one of the claims 1 to 12, having a number average molecular weight ( M_n) between 500 and 1 ,000,000 g/mol and having a polydispersity index (£>) of between 1 .1 and 1 0.0 and wherein said polyolefin block has a branching number determined by N MR of 0.2 to 1 0 per 1 0000 carbon atoms or of 50 to 3500 per 10000 carbon atoms.

14. 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 functionalized long chain branched polyolefin block and/or wherein the grafts are comprise ester and/or carbonate functionalities.

1 5. Polyolefin-based graft copolymer according to claim 13 or 14, wherein the polymer side chain(s) having a number average molecular weight (M_n) between 500 and 1 ,000,000 g/mol.