FIELD OF INVENTION

The invention relates to an ethylene polymerization process using a dual catalyst composition. This invention also relates to new ethylene polymers prepared by said process and to articles comprising said ethylene polymers.

BACKGROUND OF THE INVENTION

In the field of polymer, constant mechanical properties improvement is mandatory. It was achieved in the last few years using metallocene catalyst combined with cascade reactor to make tailor made bimodal resins. However, the requirement of multiple reactors leads to increased costs for both construction and operation, and this can be overcome using dual-site catalyst composition in a single reactor.

In the prior art, the first obvious strategy was multiple separate catalyst injection. Although, this process showed high flexibility, several drawbacks can be highlighted: multiple catalysts injections lead to increased costs and polymer homogeneity was difficult to achieve.

The strategy of using a dual-site catalyst in a single reactor seemed therefore to be a good alternative. However, this technology suffers from the difficulty to control properly the heterogenization and more importantly the activation. This might be related to the different behavior of metallocene during the heterogenization process typically leading to a dominating structure while others seem inactive. Moreover, in several examples in the literature, some combinations suffer of a lack of reactivity or works only in specific conditions or in a specific process. The challenge is to find the right combination of metallocenes to avoid these drawbacks.

SUMMARY OF THE INVENTION

It is therefore an object of the present invention to provide a new polymerization process using a dual catalyst system avoiding the above-mentioned drawbacks.

The present invention provides an ethylene polymerization process, the process comprising: contacting at least one dual catalyst composition with ethylene, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing said ethylene and the optional one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining an ethylene polymer, wherein the at least one dual catalyst composition comprises a first bridged metallocene with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group (preferably substituted fluorenyl group), and a second catalyst which is a bridged bis-indenyl metallocene, with one or more substitutions, wherein the one or more substituents is not on position 3 and/or 5 of each indenyl, preferably wherein at least one of the substituents is on position 2 and/or 4 of each indenyl. It is preferred that each indenyl is independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; wherein the unsubstituted or substituted aryl or heteroaryl is not on position 3 and/or 5 of the indenyl. The processes of the present invention allow the production of medium to high density polyethylene with a broad molecular weight distribution and can allow the preparation of polymers having very low melt flow indexes.

In a first aspect, the present invention provides an ethylene polymerization process, the process comprising: contacting at least one catalyst composition with ethylene, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing said ethylene and the optional one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining a polyethylene, wherein the at least one catalyst composition comprises: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; and wherein the unsubstituted or substituted aryl or heteroaryl substituent is not on position 3 and/or 5 of each indenyl, preferably each indenyl has one or more substituents on positions 2 and/or 4 of each indenyl, preferably each indenyl has one substituent on positions 2 and one substituent on position 4 of each indenyl, preferably the unsubstituted or substituted aryl or heteroaryl is on position 4 of each indenyl; and an optional activator; an optional support; and an optional co-catalyst.

In a second aspect, the present invention provides, an ethylene polymer produced by the process according to the first aspect of the invention.

The present invention also encompasses an article comprising the olefin polymer according to the second aspect.

The invention overcomes the drawbacks of the aforementioned strategies. The invention provides an ethylene polymerization process using a composition comprising a dual catalyst composition which means a catalyst particle with two metallocene active sites on a single carrier.

Blending occurs on a microscale when using the composition, leading to improvements in the homogeneity of the resulting product. The geometry and substitution patterns of both catalyst components can be used as a means to control desired properties in the resulting bimodal polymers. This has an important effect on processability when very broad bimodal molecular weight distributions are needed.

The use of the dual catalyst composition can provide polyethylene products with novel broad/bimodal molecular weight distributions, the desirable inverse comonomer incorporation, a good hydrogen response, and improved processing/mechanical properties.

The present invention therefore encompasses ethylene polymers having broad molecular weight distributions, ideal co-monomer incorporation, a good hydrogen response, and improved processing and mechanical properties.

After the polymer is produced, it may be formed into various articles, including but not limited to, pressure/temperature resistant pipes, film products, caps and closures, liners, rotomoulding, grass yarn, etc.

The independent and dependent claims set out particular and preferred features of the invention. Features from the dependent claims may be combined with features of the independent or other dependent claims as appropriate.

The present invention will now be further described. In the following passages, different aspects of the invention are defined in more detail. Each aspect so defined may be combined with any other aspect or aspects unless clearly indicated to the contrary. In particular, any feature or statement indicated as being preferred or advantageous may be combined with any other features or statements indicated as being preferred or advantageous.

BRIEF DESCRIPTION OF THE FIGURES

Figure 1 represents a graph plotting the ¹³ C{ ¹ H} NMR spectrum of a metallocene ethylene polymer.

Figure 2 represents a graph plotting the GPC traces (i.e., the molecular weight distribution (logarithm of molecular weight)) of the polymers obtained with Met1/Met2 compositions with varying weight ratio of each catalyst.

Figure 3 represents a graph plotting the GPC traces (i.e., the molecular weight distribution (logarithm of molecular weight)) of the polymers obtained with a 50/50 weight ratio Met1/Met2 composition.

Figure 4 represents a graph plotting the GPC trace of the copolymer obtained with Met1/Met2 (50/50 weight ratio) composition as a function of hydrogen concentration.

Figure 5 represents a graph plotting the GPC trace of the copolymer obtained with Met1/Met2 (30/70 weight ratio) composition as a function of hydrogen concentration.

Figure 6 represents a graph plotting the GPC trace of the homopolymer obtained with Met1/Met2 (50/50 weight ratio) composition as a function of hydrogen concentration. Figure 7 represents a graph plotting the GPC trace of the polymer obtained with Met1/Met3 (50/50 weight ratio) composition.

DETAILED DESCRIPTION OF THE INVENTION

Before the present compositions, compounds, polymers, processes, articles, and uses encompassed by the invention are described, it is to be understood that this invention is not limited to particular compositions, compounds, polymers, processes, articles, and uses described, as such compositions, compounds, polymers, processes, articles, and uses may, of course, vary. It is also to be understood that the terminology used herein is not intended to be limiting, since the scope of the present invention will be limited only by the appended claims.

Unless otherwise defined, all terms used in disclosing the invention, including technical and scientific terms, have the meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. By means of further guidance, definitions for the terms used in the description are included to better appreciate the teaching of the present invention. When describing the compounds, processes, articles, and uses of the invention, the terms used are to be construed in accordance with the following definitions, unless the context dictates otherwise.

As used herein, the singular forms "a", "an", and "the" include both singular and plural referents unless the context clearly dictates otherwise. By way of example, "a polymer" means one polymer or more than one polymer.

The terms "comprising", "comprises" and "comprised of" as used herein are synonymous with "including", "includes" or "containing", "contains", and are inclusive or open-ended and do not exclude additional, non-recited members, elements or method steps. The terms "comprising", "comprises" and "comprised of" also include the term “consisting of”.

The recitation of numerical ranges by endpoints includes all integer numbers and, where appropriate, fractions subsumed within that range (e.g., 1 to 5 can include 1 , 2, 3, 4 when referring to, for example, a number of elements, and can also include 1.5, 2, 2.75 and 3.80, when referring to, for example, measurements). The recitation of end points also includes the end point values themselves (e.g., from 1.0 to 5.0 includes both 1.0 and 5.0). Any numerical range recited herein is intended to include all sub-ranges subsumed therein.

Reference throughout this specification to “one embodiment” or “an embodiment” means that a particular feature, structure or characteristic described in connection with the embodiment is included in at least one embodiment of the present invention. Thus, appearances of the phrases “in one embodiment” or “in an embodiment” in various places throughout this specification are not necessarily all referring to the same embodiment, but may. Furthermore, the particular features, structures or characteristics may be combined in any suitable manner, as would be apparent to a person skilled in the art from this disclosure, in one or more embodiments. Furthermore, while some embodiments described herein include some but not other features included in other embodiments, combinations of features of different embodiments are meant to be within the scope of the invention, and form different embodiments, as would be understood by those in the art. For example, in the following claims and statements, any of the embodiments can be used in any combination.

Whenever the term “substituted” is used herein, it is meant to indicate that one or more hydrogen atoms on the atom indicated in the expression using “substituted” is replaced with a selection from the indicated group, provided that the indicated atom’s normal valence is not exceeded, and that the substitution results in a chemically stable compound, i.e., a compound that is sufficiently robust to survive isolation from a reaction mixture. Preferred substituents for the indenyl, cyclopentadienyl and fluorenyl groups, can be selected from the group comprising alkyl, alkenyl, cycloalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, heteroalkyl; wherein each R ¹⁰ is independently hydrogen, alkyl, or alkenyl. Preferably, each indenyl is substituted with at least one aryl or heteroaryl, more preferably aryl; preferably wherein the aryl or heteroaryl substituent is on the 3-position on each indenyl; the indenyl can be further substituted with one or more substituents selected from the group comprising alkyl, alkenyl, cycloalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, heteroalkyl; wherein each R ¹⁰ is independently hydrogen, alkyl, or alkenyl.

The term “halo” or “halogen” as a group or part of a group is generic for fluoro, chloro, bromo, iodo.

The term "alkyl" as a group or part of a group, refers to a hydrocarbyl group of formula C _n H2n+i wherein n is a number greater than or equal to 1 . Alkyl groups may be linear or branched and may be substituted as indicated herein. Generally, alkyl groups of this invention comprise from 1 to 20 carbon atoms, preferably from 1 to 10 carbon atoms, preferably from 1 to 6 carbon atoms, more preferably from 1 to 4 carbon atoms. When a subscript is used herein following a carbon atom, the subscript refers to the number of carbon atoms that the named group may contain. For example, the term "Ci-2oalkyl", as a group or part of a group, refers to a hydrocarbyl group of formula -C _n H2n+i wherein n is a number ranging from 1 to 20. Thus, for example, “Cisalkyl” includes all linear or branched alkyl groups with between 1 and 8 carbon atoms, and thus includes methyl, ethyl, n-propyl, i-propyl, butyl and its isomers (e.g., n-butyl, i-butyl and t- butyl); pentyl and its isomers, hexyl and its isomers, etc. A “substituted alkyl" refers to an alkyl group substituted with one or more substituent(s) (for example 1 to 3 substituent(s), for example 1 , 2, or 3 substituent(s)) at any available point of attachment.

When the suffix "ene" is used in conjunction with an alkyl group, i.e., “alkylene”, this is intended to mean the alkyl group as defined herein having two single bonds as points of attachment to other groups. As used herein, the term “alkylene” also referred as “alkanediyl”, by itself or as part of another substituent, refers to alkyl groups that are divalent, i.e. , with two single bonds for attachment to two other groups. Alkylene groups may be linear or branched and may be substituted as indicated herein. Non-limiting examples of alkylene groups include methylene (-CH2-), ethylene (-CH2-CH2-), methylmethylene (-CH(CH3)-), 1-methyl-ethylene (-CH(CH3)- CH2-), n-propylene (-CH2-CH2-CH2-), 2-methylpropylene (-CH2-CH(CH3)-CH2-), 3- methylpropylene (-CH2-CH2-CH(CH3)-), n-butylene (-CH2-CH2-CH2-CH2-), 2-methylbutylene (- CH2-CH(CH ₃ )-CH2-CH ₂ -), 4-methylbutylene (-CH2-CH ₂ -CH2-CH(CH ₃ )-), pentylene and its chain isomers, hexylene and its chain isomers.

The term “alkenyl” as a group or part of a group, refers to an unsaturated hydrocarbyl group, which may be linear, or branched, comprising one or more carbon-carbon double bonds. Generally, alkenyl groups of this invention comprise from 3 to 20 carbon atoms, preferably from 3 to 10 carbon atoms, preferably from 3 to 8 carbon atoms. When a subscript is used herein following a carbon atom, the subscript refers to the number of carbon atoms that the named group may contain. Examples of C3-2oalkenyl groups are ethenyl, 2-propenyl, 2-butenyl, 3-butenyl, 2-pentenyl and its isomers, 2-hexenyl and its isomers, 2,4-pentadienyl, and the like.

The term “alkoxy" or “alkyloxy”, as a group or part of a group, refers to a group having the formula -OR ^b wherein R ^b is alkyl as defined herein above. Non-limiting examples of suitable alkoxy include methoxy, ethoxy, propoxy, isopropoxy, butoxy, isobutoxy, sec-butoxy, tertbutoxy, pentyloxy and hexyloxy.

The term “cycloalkyl”, as a group or part of a group, refers to a cyclic alkyl group, that is a monovalent, saturated, hydrocarbyl group having 1 or more cyclic structure, and comprising from 3 to 20 carbon atoms, more preferably from 3 to 10 carbon atoms, more preferably from 3 to 8 carbon atoms; more preferably from 3 to 6 carbon atoms. Cycloalkyl includes all saturated hydrocarbon groups containing 1 or more rings, including monocyclic, bicyclic groups or tricyclic. The further rings of multi-ring cycloalkyls may be either fused, bridged and/or joined through one or more spiro atoms. When a subscript is used herein following a carbon atom, the subscript refers to the number of carbon atoms that the named group may contain. For example, the term “C3-2ocycloalkyl”, a cyclic alkyl group comprising from 3 to 20 carbon atoms. For example, the term “Cs- cycloalkyl”, a cyclic alkyl group comprising from 3 to 10 carbon atoms. For example, the term “Cs-scycloalkyl”, a cyclic alkyl group comprising from 3 to 8 carbon atoms. For example, the term “Cs-ecycloalkyl”, a cyclic alkyl group comprising from 3 to 6 carbon atoms. Examples of C3-i2cycloalkyl groups include but are not limited to adamantly, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, bicycle[2.2.1]heptan-2yl, (1S,4R)-norbornan-2-yl, (1 R,4R)-norbornan-2-yl, (1S,4S)-norbornan- 2-yl, (1 R,4S)-norbornan-2-yl. When the suffix "ene" is used in conjunction with a cycloalkyl group, i.e., cycloalkylene, this is intended to mean the cycloalkyl group as defined herein having two single bonds as points of attachment to other groups. Non-limiting examples of "cycloalkylene" include 1 ,2- cyclopropylene, 1 ,1 -cyclopropylene, 1 ,1 -cyclobutylene, 1 ,2-cyclobutylene, 1 ,3-cyclopentylene, 1 ,1 -cyclopentylene, and 1 ,4-cyclohexylene.

Where an alkylene or cycloalkylene group is present, connectivity to the molecular structure of which it forms part may be through a common carbon atom or different carbon atom. To illustrate this applying the asterisk nomenclature of this invention, a C ₃ alkylene group may be for example *-CH ₂ CH ₂ CH ₂ -*, *-CH(-CH ₂ CH ₃ )-* or *-CH ₂ CH(-CH ₃ )-*. Likewise, a C ₃ cycloalkylene group may be

The term “cycloalkenyl” as a group or part of a group, refers to a non-aromatic cyclic alkenyl group, with at least one site (usually 1 to 3, preferably 1) of unsaturation, namely a carboncarbon, sp2 double bond; preferably having from 5 to 20 carbon atoms more preferably from 5 to 10 carbon atoms, more preferably from 5 to 8 carbon atoms, more preferably from 5 to 6 carbon atoms. Cycloalkenyl includes all unsaturated hydrocarbon groups containing 1 or more rings, including monocyclic, bicyclic or tricyclic groups. The further rings may be either fused, bridged and/or joined through one or more spiro atoms. When a subscript is used herein following a carbon atom, the subscript refers to the number of carbon atoms that the named group may contain. For example, the term “Cs-2ocycloalkenyl”, a cyclic alkenyl group comprising from 5 to 20 carbon atoms. For example, the term “Cs- cycloalkenyl”, a cyclic alkenyl group comprising from 5 to 10 carbon atoms. For example, the term “Cs-scycloalkenyl”, a cyclic alkenyl group comprising from 5 to 8 carbon atoms. For example, the term “Cs- ecycloalkyl”, a cyclic alkenyl group comprising from 5 to 6 carbon atoms. Examples include but are not limited to: cyclopentenyl (-C5H7), cyclopentenylpropylene, methylcyclohexenylene and cyclohexenyl (-CeHg). The double bond may be in the cis or trans configuration.

The term "cycloalkenylalkyl", as a group or part of a group, means an alkyl as defined herein, wherein at least one hydrogen atom is replaced by at least one cycloalkenyl as defined herein.

The term “cycloalkoxy”, as a group or part of a group, refers to a group having the formula - OR ^h wherein R ^h is cycloalkyl as defined herein above.

The term “aryl”, as a group or part of a group, refers to a polyunsaturated, aromatic hydrocarbyl group having a single ring (i.e., phenyl) or multiple aromatic rings fused together (e.g., naphthyl), or linked covalently, typically containing 6 to 20 atoms; preferably 6 to 10, wherein at least one ring is aromatic. The aromatic ring may optionally include one to two additional rings (either cycloalkyl, heterocyclyl or heteroaryl) fused thereto. Examples of suitable aryl include Ce-2oaryl, preferably Ce- aryl, more preferably Ce-saryl. Non-limiting examples of aryl comprise phenyl, biphenylyl, biphenylenyl, or 1-or2-naphthanelyl; 1-, 2-, 3-, 4-, 5- or 6-tetralinyl (also known as “1 ,2,3,4-tetrahydronaphtalene); 1-, 2-, 3-, 4-, 5-, 6-, 7- or 8-azulenyl, 4-, 5-, 6 or 7-indenyl; 4- or 5-indanyl; 5-, 6-, 7- or 8-tetrahydronaphthyl; 1 ,2,3,4-tetrahydronaphthyl; and 1 ,4-dihydronaphthyl; 1-, 2-, 3-, 4- or 5-pyrenyl. A “substituted aryl” refers to an aryl group having one or more substituent(s) (for example 1 , 2 or 3 substituent(s), or 1 to 2 substituent(s)), at any available point of attachment.

The term “aryloxy”, as a group or part of a group, refers to a group having the formula -OR ^g wherein R ^g is aryl as defined herein above.

The term "arylalkyl", as a group or part of a group, means an alkyl as defined herein, wherein at least one hydrogen atom is replaced by at least one aryl as defined herein. Non-limiting examples of arylalkyl group include benzyl, phenethyl, dibenzylmethyl, methylphenylmethyl, 3- (2-naphthyl)-butyl, and the like.

The term “alkylaryl” as a group or part of a group, means an aryl as defined herein wherein at least one hydrogen atom is replaced by at least one alkyl as defined herein. Non-limiting example of alkylaryl group include p-CH3-R ^g -, wherein R ^g is aryl as defined herein above.

The term “arylalkyloxy” or “aralkoxy” as a group or part of a group, refers to a group having the formula -O-R ^a -R ^g wherein R ^g is aryl, and R ^a is alkylene as defined herein above.

The term “heteroalkyl” as a group or part of a group, refers to an acyclic alkyl wherein one or more carbon atoms are replaced by at least one heteroatom selected from the group comprising O, Si, S, B, and P, with the proviso that said chain may not contain two adjacent heteroatoms. This means that one or more -CH3 of said acyclic alkyl can be replaced by -OH for example and/or that one or more -CR2- of said acyclic alkyl can be replaced by O, Si, S, B, and P.

The term “aminoalkyl” as a group or part of a group, refers to the group -R ^j -NR ^k R' wherein R ^j is alkylene, R ^k is hydrogen or alkyl as defined herein, and R ¹ is hydrogen or alkyl as defined herein.

The term "heterocyclyl" as a group or part of a group, refers to non-aromatic, fully saturated or partially unsaturated cyclic groups (for example, 3 to 7 membered monocyclic group, 7 to 10 membered bicyclic group) preferably containing a total of 3 to 10 ring atoms, which have at least one heteroatom in at least one carbon atom-containing ring. Each ring of the heterocyclic group containing a heteroatom may have 1 , 2, 3 or 4 heteroatoms selected from N, S, Si, Ge, where the nitrogen and sulfur heteroatoms may optionally be oxidized and the nitrogen heteroatoms may optionally be quaternized. The heterocyclic group may be attached at any heteroatom or carbon atom of the ring or ring system, where valence allows. The rings of multiring heterocycles may be fused, bridged and/or joined through one or more spiro atoms.

Non limiting exemplary heterocyclic groups include aziridinyl, oxiranyl, thiiranyl, piperidinyl, azetidinyl, 2-imidazolinyl, pyrazolidinyl imidazolidinyl, isoxazolinyl, oxazolidinyl, isoxazolidinyl, thiazolidinyl, isothiazolidinyl, piperidinyl, succinimidyl, 3H-indolyl, indolinyl, isoindolinyl, 2H- pyrrolyl, 1 -pyrrolinyl, 2-pyrrolinyl, 3-pyrrolinyl, pyrrolidinyl, 4H-quinolizinyl, 2-oxopiperazinyl, piperazinyl, homopiperazinyl, 2-pyrazolinyl, 3-pyrazolinyl, tetrahydro-2H-pyranyl, 2H-pyranyl, 4H-pyranyl, 3,4-dihydro-2H-pyranyl, oxetanyl, thietanyl, 3-dioxolanyl, 1 ,4-dioxanyl, 2,5- dioximidazolidinyl, 2-oxopiperidinyl, 2-oxopyrrolodinyl, indolinyl, tetrahydropyranyl, tetrahydrofuranyl, tetrahydrothiophenyl, tetrahydroquinolinyl, tetrahydroisoquinolin-1-yl, tetrahydroisoquinolin-2-yl, tetrahydroisoquinolin-3-yl, tetrahydroisoquinolin-4-yl, thiomorpholin-4-yl, thiomorpholin-4-ylsulfoxide, thiomorpholin-4-ylsulfone, 1 , 3-dioxolanyl, 1 ,4- oxathianyl, 1 ,4-dithianyl, 1 ,3,5-trioxanyl, 1 H-pyrrolizinyl, tetrahydro-1 ,1 -dioxothiophenyl, N- formylpiperazinyl, and morpholin-4-yl.

Whenever used in the present invention the term “compounds” or a similar term is meant to include the compounds of general formula (I) and/or (II) and any subgroup thereof, including all polymorphs and crystal habits thereof, and isomers thereof (including optical, geometric and tautomeric isomers) as hereinafter defined.

The compounds of formula (I) and/or (I I) or any subgroups thereof may comprise alkenyl group, and the geometric cis/trans (or Z/E) isomers are encompassed herein. Where structural isomers are interconvertible via a low energy barrier, tautomeric isomerism ('tautomerism') can occur. This can take the form of proton tautomerism in compounds of formula (I) containing, for example, a keto group, or so-called valence tautomerism in compounds which contain an aromatic moiety. It follows that a single compound may exhibit more than one type of isomerism.

Cis/trans isomers may be separated by conventional techniques well known to those skilled in the art, for example, chromatography and fractional crystallization.

Preferred statements (features) and embodiments of the compositions, processes, polymers, articles, and uses of this invention are set herein below. Each statement and embodiment of the invention so defined may be combined with any other statement and/or embodiment, unless clearly indicated to the contrary. In particular, any feature indicated as being preferred or advantageous may be combined with any other features or statements indicated as being preferred or advantageous. Hereto, the present invention is in particular captured by any one or any combination of one or more of the below numbered statements and embodiments, with any other aspect and/or embodiment.

1. An ethylene polymerization process, the process comprising: contacting at least one catalyst composition with ethylene, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing said ethylene and the optional one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining a polyethylene, wherein the at least one catalyst composition comprises: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; and wherein the unsubstituted or substituted aryl or heteroaryl is not on position 3 and/or 5 of each indenyl, preferably not on position 3 and 5 of each indenyl; preferably each indenyl has one or more substituents on positions 2 and/or 4 of each indenyl, preferably each indenyl has one substituent on position 2, preferably each indenyl has one substituent on position 4, yet more preferably each indenyl has one substituent on positions 2 and one substituent on position 4 of each indenyl, preferably the unsubstituted or substituted aryl or heteroaryl is on position 4 of each indenyl; and an optional activator; an optional support; and an optional co-catalyst. An ethylene polymerization process, the process comprising: contacting at least one catalyst composition with ethylene, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing said ethylene and the optional one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining a polyethylene, wherein the at least one catalyst composition comprises: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups, each indenyl being independently substituted with two or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; each indenyl having at least one substituent on positions 2 and/or 4 of each indenyl, preferably each indenyl has one substituent on position 2, preferably each indenyl has one substituent on position 4, yet more preferably each indenyl has one substituent on positions 2 and one substituent on position 4 of each indenyl, preferably said unsubstituted or substituted aryl substituent on position 4 of each indenyl; and an optional activator; an optional support; and an optional co-catalyst. 3. An ethylene polymerization process, the process comprising: contacting at least one catalyst composition with ethylene, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing said ethylene and the optional one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining a polyethylene, wherein the at least one catalyst composition comprises: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups, each indenyl being independently substituted with two or more substituents, wherein one of the substituents is on position 2 of each indenyl and one other substituent is on position 4 of each indenyl, preferably wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; preferably wherein the unsubstituted or substituted aryl or heteroaryl is on the 4-position of each indenyl; preferably wherein the other substituents are not on position 3 and/or 5 of the indenyl; and an optional activator; an optional support; and an optional co-catalyst.

4. An ethylene polymerization process, the process comprising: contacting at least one catalyst composition with ethylene, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing said ethylene and the optional one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining a polyethylene, wherein the at least one catalyst composition comprises: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; wherein the unsubstituted or substituted aryl or heteroaryl is on position 4 of each indenyl; and an optional activator; an optional support; and an optional co-catalyst.

5. The process according to any one of statements 1-4, wherein the weight ratio of catalyst component A to catalyst component B is in a range of from 10/90 to 90/10, preferably in the range of from 20/80 to 80/20, preferably in the range of from 30/70 to 70/30, preferably in the range of from 40/60 to 60/40, preferably in the range of from 45/55 to 55/45.

6. The process according to any one of statements 1-5, wherein the bridged metallocene compound of catalyst component A comprises at least one alkenyl, cycloalkenyl, or cycloalkenylalkyl substituent, preferably at least one C3-2oalkenyl, Cs-2ocycloalkenyl, or Ce- 2ocycloalkenylalkyl substituent, more preferably at least one Cs-salkenyl, Cs-scycloalkenyl, or Ce-scycloalkenylalkyl substituent.

7. The process according to any one of statements 1-6, wherein the bridged metallocene compound of catalyst component A comprises at least one alkenyl, cycloalkenyl, or cycloalkenylalkyl substituent on the bridge; preferably at least one C3-2oalkenyl, Cs- 2ocycloalkenyl, or C6-2ocycloalkenylalkyl substituent, more preferably at least one C3- salkenyl, Cs-scycloalkenyl, or Ce-scycloalkenylalkyl substituent.

8. The process according to any one of statements 1-7, wherein catalyst component B contains a Si, or C bridging atom, optionally substituted with a one or two substituents each independently selected from alkyl, alkenyl, cycloalkyl, or cycloalkenyl.

9. The process according to any one of statements 1-8, wherein catalyst component A contains a C, Si, B or Ge bridging atom.

10. The process according to any one of statements 1-9, wherein the activator comprises an aluminoxane compound, an organoboron or organoborate compound, an ionizing ionic compound, or any combination thereof, preferably wherein the activator comprises an alumoxane compound.

11 . The process according to any one of statements 1-10, wherein the activator comprises at least one alumoxane compound of formula (V) or (VI)

R ^a -(AI(R ^a )-O) _x -AIR ^a 2 (V) for oligomeric, linear alumoxanes; or

(-AI(R ^a )-O-) _y (VI) for oligomeric, cyclic alumoxanes wherein x is 1-40, and preferably 10-20; wherein y is 3-40, and preferably 3-20; and wherein each R ^a is independently selected from a Ci-salkyl, and preferably is methyl.

12. The process according to any one of statements 1-11 , wherein the activator is methyl alumoxane.

13. The process according to any one of statements 1-12, wherein the catalyst composition comprises a co-catalyst.

14. The process according to any one of statements 1-13, wherein the catalyst composition comprises an organoaluminum co-catalyst.

15. The process according to any one of statements 1-14, wherein the catalyst composition comprises an organoaluminum co-catalyst selected from the group comprising trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, diisobutylaluminum hydride, diethylaluminum ethoxide, diethylaluminum chloride, and any combination thereof. The process according to any one of statements 1-15, wherein the support comprises a solid oxide, preferably a solid inorganic oxide, preferably, the solid oxide comprises titanated silica, silica, alumina, silica-alumina, silica-coated alumina, aluminum phosphate, aluminophosphate, heteropolytungstate, titania, zirconia, magnesia, boria, zinc oxide, a mixed oxide thereof, or any mixture thereof; preferably silica, titanated silica, silica treated with fluoride, silica-alumina, alumina treated with fluoride, sulfated alumina, silica-alumina treated with fluoride, sulfated silica-alumina, silica-coated alumina, silica treated with fluoride, sulfated silica-coated alumina, or any combination thereof. The process according to any one of statements 1-16, wherein the support has a D50 of at most 50 pm, preferably of at most 40 pm, preferably of at most 30 pm. The D50 is defined as the particle size for which fifty percent by weight of the particles has a size lower than the D50. The particle size may be measured by laser diffraction analysis on a Malvern type analyzer. The process according to any one of statements 1-17, comprising an alumoxane activator; and a titanated silica or silica solid support; and an optional co-catalyst. The process to any one of statements 1-18, wherein catalyst component A comprises a bridged metallocene of formula (I), wherein each of R ⁵ , R ⁶ , and R ⁷ , are independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each R ¹⁰ is independently hydrogen, alkyl, or alkenyl; and r, s, t are each independently an integer selected from 0, 1 , 2, 3, or 4;

L ² is -[CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, aminoalkyl, and arylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a cycloalkyl, cycloalkenyl or heterocyclyl;

M ² is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably is zirconium; and

Q ³ and Q ⁴ are each independently selected from the group comprising halogen, alkyl, - N(R ¹¹ ) ₂ , alkoxy, cycloalkoxy, aralkoxy, cycloalkyl, aryl, alkylaryl, aralkyl, and heteroalkyl; wherein R ¹¹ is hydrogen or alkyl.

20. The process according to any one of statements 1-19, wherein catalyst component A comprises a bridged metallocene of formula (I), wherein each of R ⁵ , R ⁶ , and R ⁷ , are independently selected from the group consisting of Ci-2oalkyl, C3-2oalkenyl, C3-2ocycloalkyl, Cs-2ocycloalkenyl, Ce-2ocycloalkenylalkyl, Ce-2oaryl, Ci-2oalkoxy, C7-2oalkylaryl, C7-2oarylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-2oalkyl; wherein each R ¹⁰ is independently hydrogen, Ci-2oalkyl, or C3-2oalkenyl; and r, s, t are each independently an integer selected from 0, 1 , 2, 3, or 4;

L ² is -[CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group consisting of hydrogen, Ci- 2oalkyl, C3-2oalkenyl, C3-20 cycloalkyl, Cs-2ocycloalkenyl, C6-2ocycloalkenylalkyl, Ce-waryl, aminoCi-ealkyl, and C?-C2oarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a C3-2ocycloalkyl, Cs-2ocycloalkenyl or heterocyclyl;

M ² is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably is zirconium; and

Q ³ and Q ⁴ are each independently selected from the group comprising halogen, Ci-2oalkyl , -N(R ¹¹ ) ₂ , Ci-2oalkoxy, C3-2ocycloalkoxy, C?-2oaralkoxy, C3-2ocycloalkyl, Ce-2oaryl, C7- 2oalkylaryl, C?-2oaralkyl, and heteroCi-2oalkyl; wherein R ¹¹ is hydrogen or Ci-2oalkyl.

21 . The process according to any one of statements 19-20, wherein each of R ⁵ , R ⁶ , and R ⁷ , are independently selected from the group comprising Ci-salkyl, C3- salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Ce-scycloalkenylalkyl, Ce- aryl, Ciwalkoxy, C7- i ₂ alkylaryl, C7-i2arylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-salkyl; wherein each R ¹⁰ is independently hydrogen, Ci-salkyl, or Cs-salkenyl; and r, s, t are each independently an integer selected from 0, 1 , 2, 3, or 4;

L ² is -[CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Cisalkyl, Cs-salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Cs-scycloalkenylalkyl, Ce-waryl, aminoCi-ealkyl, and CyCwarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a Cs-scycloalkyl, Cs-scycloalkenyl or heterocyclyl;

M ² is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably is zirconium; and

Q ³ and Q ⁴ are each independently selected from the group comprising halogen, Ci-salkyl, -N(R ¹¹ ) ₂ , Ci-salkoxy, Cs-scycloalkoxy, C7-i2aralkoxy, Cs-scycloalkyl, Ce- aryl, Cy- alkylaryl, Cy-waralkyl, and heteroCiwalkyl; wherein R ¹¹ is hydrogen or Ci-salkyl. The process according to any one of statements 19-21 , wherein each of R ⁵ , R ⁶ , and R ⁷ , is independently selected from the group comprising Ci-salkyl, Cs- salkenyl, Cs-scycloalkyl, Ce- aryl, and halogen; and r, s, t are each independently an integer selected from 0, 1 , 2, 3, or 4; preferably 0, 1 , 2, or 3, preferably 0, 1 , or 2; preferably 0, or 1 ;

L ² is -[CR ⁸ R ⁹ ]h-, or SiR ⁸ R ⁹ ; wherein h is an integer selected from 1 , or 2; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-salkyl , Cs-salkenyl, Cs-scycloalkyl; Cs-scycloalkenyl, Cs-scycloalkenylalkyl, and Ce-waryl;

M ² is a transition metal selected from zirconium, or hafnium; and preferably zirconium; and

Q ³ and Q ⁴ are each independently selected from the group comprising halogen, Ci-salkyl, -N(R ¹¹ ) ₂ , Ce-waryl, and Cy-waralkyl; wherein R ¹¹ is hydrogen or Ci-salkyl, preferably Q ¹ and Q ² are each independently selected from the group comprising Cl, F, Br, I, methyl, benzyl, and phenyl. The process according to any one of statements 1-22, wherein catalyst component A comprises a bridged metallocene of formula (la), wherein R ⁵ , R ⁶ , R ⁷ , L ² , M ² , Q ³ , Q ⁴ , and r have the same meaning as that defined in any one of statements 19-22, preferably each R ⁶ and R ⁷ is Ci-salkyl. The process according to any one of statements 1-23, wherein catalyst component A comprises a bridged metallocene of formula (lb), wherein R ⁶ , R ⁷ , L ² , M ² , Q ³ , Q ⁴ , have the same meaning as that defined in any one of statements 19-22, preferably each R ⁶ and R ⁷ is Ci-salkyl. The process according to any one of statements 1-24, wherein catalyst component A comprises a bridged metallocene of formula (Ic), wherein R ⁶ , R ⁷ , R ⁸ , R ⁹ , M ² , Q ³ , Q ⁴ , have the same meaning as that defined in any one of statements 19-22, preferably each R ⁶ and R ⁷ is Ci-salkyl. The process according to any one of statements 1-25, wherein catalyst component A comprises a bridged metallocene of formula (Id), The process according to any one of statements 1-25, wherein catalyst component B comprises a bridged metallocene catalyst of formula (II), wherein each of R ¹ , and R ³ , are independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each of said group can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, alkoxy, halogen, haloalkyl; wherein at least one of R ¹ or R ³ is unsubstituted or substituted aryl, wherein each R ¹⁰ is independently hydrogen, alkyl, aryl, or alkenyl; and m, p, are each independently an integer selected from 0, 1 , 2, 3, or 4, wherein at least one of m or p is at least 1 ; each of R ² , and R ⁴ , are independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, cycloalkenyl, cycloalkenylalkyl, phenyl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each of said group can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, alkoxy, halogen, haloalkyl; wherein at least one of R ² or R ⁴ is unsubstituted or substituted aryl, wherein each R ¹⁰ is independently hydrogen, alkyl, aryl, or alkenyl; and n, q are each independently an integer selected from 0, 1 , 2, 3, or 4, wherein at least one of n or q is at least 1 ;

L ¹ is SiR ⁸ R ⁹ , -[CR ⁸ R ⁹ ]h-, GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, aminoalkyl, and arylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a cycloalkyl, cycloalkenyl or heterocyclyl;

M ¹ is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably M is zirconium; and

Q ¹ and Q ² are each independently selected from the group comprising hydrogen, halogen, hydroxyl, alkyl, alkenyl, -N(R ¹¹ )2, -SR ¹¹ , alkoxy, cycloalkoxy, aralkoxy, cycloalkyl, aryl, aryloxy, alkylaryl, aralkyl, and heteroalkyl; wherein R ¹¹ is hydrogen, alkyl or aryl. The process according to any one of statements 1-27, wherein the catalyst component B contains a SiR ⁸ R ⁹ , or -[CR ⁸ R ⁹ ]h- bridging group; preferably a SiR ⁸ R ⁹ bridging group; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, aminoalkyl, and arylalkyl, preferably alkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a cycloalkyl, cycloalkenyl or heterocyclyl. The process according to any one of statements 1-28, wherein catalyst component B comprises a bridged metallocene of formula (Ila), wherein R ¹ , R ² , R ³ , R ⁴ , L ¹ , M ¹ , Q ¹ , Q ² , m and n have the same meaning as that defined in any one of statements 27-28, preferably wherein R ³ and R ⁴ are each independently Ce- aryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Ci-ealkoxy, halogen, haloCi- ealkyl. The process according to any one of statements 27-29, wherein

R ¹ is selected from the group comprising Ci-2oalkyl, C3-2oalkenyl, C3-2ocycloalkyl, Cs- 2ocycloalkenyl, C6-2ocycloalkenylalkyl, Ce-2oaryl, Ci-2oalkoxy, C?-2oalkylaryl, C?-2oarylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-^alkyl; wherein each of said group can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, Cs-ecycloalkylCi-ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl; wherein each R ¹⁰ is independently hydrogen, Ci-2oalkyl, or C3- 2oalkenyl; and m is an integer selected from 0, or 1 , preferably m is 1 ;

R ³ is Ce-2oaryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, C3- ecycloalkylCi-ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl, preferably R ³ is phenyl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, Cs-ecycloalkylCi-ealkyl, Ci- ealkoxy, halogen, haloCi-ealkyl;

R ² is selected from the group comprising Ci-2oalkyl, C3-2oalkenyl, C3-2ocycloalkyl, C5- 2ocycloalkenyl, Ce-2ocycloalkenylalkyl, Ce-2oaryl, Ci-2oalkoxy, C?-2oalkylaryl, C?-2oarylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-^alkyl; wherein each of said group can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, Cs-ecycloalkylCi-ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl; wherein each R ¹⁰ is independently hydrogen, Ci-2oalkyl, or C3- 2oalkenyl; and n is an integer selected from 0, or 1 , preferably n is 1 ;

R ⁴ is Ce-2oaryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, C3- ecycloalkylCi-ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl, preferably R ⁴ is phenyl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, Cs-ecycloalkylCi-ealkyl, Ci- ealkoxy, halogen, haloCi-ealkyl;

L ¹ is SiR ⁸ R ⁹ , or -[CR ⁸ R ⁹ ]h-, wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-2oalkyl , C3-2oalkenyl, C3-20 cycloalkyl, Cs-2ocycloalkenyl, Ce-2ocycloalkenylalkyl, Ce-waryl, aminoCi-ealkyl, and C7- C2oarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a C3- 2ocycloalkyl, Cs-2ocycloalkenyl or heterocyclyl; preferably L ¹ is SiR ⁸ R ⁹ ; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-2oalkyl, C3-2oalkenyl, C3-20 cycloalkyl, Cs-2ocycloalkenyl, C6-2ocycloalkenylalkyl, Ce- aryl, aminoCi-ealkyl, and C7- C2oarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a C3- 2ocycloalkyl, Cs-2ocycloalkenyl or heterocyclyl; preferably each of R ⁸ , and R ⁹ are independently Ci-ealkyl;

M ¹ is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably M is zirconium; and

Q ¹ and Q ² are each independently selected from the group consisting of hydrogen, halogen, Ci-2oalkyl, -N(R ¹¹ )2, Ci-2oalkoxy, C3-2ocycloalkoxy, C7-2oaralkoxy, C3-2ocycloalkyl, Ce-2oaryl, C7-2oalkylaryl, C7-2oaralkyl, and heteroCi-2oalkyl; wherein R ¹¹ is hydrogen or C1- 2oalkyl. The process according to any one of statements 27-30, wherein

R ¹ is selected from the group comprising Ci- alkyl, Cs-walkenyl, Ce- aryl, Ci-walkoxy, halogen, and heteroCi-walkyl; preferably R ¹ is Ci-salkyl;

R ³ is Ce-waryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, C3- ecycloalkylCi-ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl, preferably R ³ is phenyl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, Cs-ecycloalkylCi-ealkyl, Ci- ealkoxy, halogen, haloCi-ealkyl; m is an integer selected from 0, or 1 , preferably m is 1 ; R ² is selected from the group comprising Ci- alkyl, C2- alkenyl, Ce-waryl, Ci-walkoxy, halogen, and heteroCi-walkyl; preferably R ² is Ci-salkyl;

R ⁴ is Ce- aryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, C3- ecycloalkylCi-ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl, preferably R ⁴ is phenyl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Cs-ecycloalkyl, Cs-ecycloalkylCi-ealkyl, Ci- ealkoxy, halogen, haloCi-ealkyl; n is an integer selected from 0, or 1 , preferably n is 1 ;

L ¹ is SiR ⁸ R ⁹ , -[CR ⁸ R ⁹ ]h-; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-salkyl , Cs-salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Ce-scycloalkenylalkyl, Ce- aryl, aminoCi-ealkyl, and C7- Cwarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a C3- scycloalkyl, Cs-scycloalkenyl or heterocyclyl; preferably L ¹ is SiR ⁸ R ⁹ ; preferably each of R ⁸ , and R ⁹ are independently selected from hydrogen, or Ci-salkyl;

M ¹ is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably M is zirconium; and

Q ¹ and Q ² are each independently selected from the group comprising hydrogen, halogen, Ci-salkyl, -N(R ¹¹ ) ₂ , Ci-salkoxy, Cswcycloalkoxy, Cy-waralkoxy, Cs-scycloalkyl, Ce-waryl, C7- walkylaryl, Cy-waralkyl, and heteroCiwalkyl; wherein R ¹¹ is hydrogen or Ci-salkyl. The process according to any one of statements 27-31 , wherein

R ¹ is selected from the group comprising Ci-salkyl , Cs-salkenyl, Cs-scycloalkyl, Ce-waryl, and halogen; preferably R ¹ is Ci-salkyl;

R ³ is Ce-waryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Ci-ealkoxy, halogen, haloCi-ealkyl, preferably R ³ is phenyl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci- ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl; m is an integer selected from 0, or 1 , preferably m is 1 ;

R ² is selected from the group comprising Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Ce-waryl, and halogen; preferably R ² is Ci-salkyl;

R ⁴ is Ce-waryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Cs-ealkenyl, Ci-ealkoxy, halogen, haloCi-ealkyl, preferably R ⁴ is phenyl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci- ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl; n is an integer selected from 0, or 1 , preferably n is 1 ;

L ¹ is SiR ⁸ R ⁹ , or -[CR ⁸ R ⁹ ]h-; wherein h is an integer selected from 1 , or 2; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-salkyl , Cswalkenyl, Cs-scycloalkyl; Cs-scycloalkenyl, Ce-scycloalkenylalkyl, and Ce- aryl; preferably L ¹ is SiR ⁸ R ⁹ ; preferably each of R ⁸ , and R ⁹ are independently selected from hydrogen, or Ci-salkyl;

M ¹ is a transition metal selected from zirconium, or hafnium; and preferably M is zirconium; and

Q ¹ and Q ² are each independently selected from the group comprising hydrogen, halogen, Ci-salkyl, -N(R ¹¹ ) ₂ , Ce- aryl, and Cy-waralkyl; wherein R ¹¹ is hydrogen or Ci-salkyl, preferably Q ¹ and Q ² are each independently selected from the group comprising Cl, F, Br, I, methyl, benzyl, and phenyl. The process according to any one of statements 1-32, wherein catalyst component B comprises bridged metallocene of formula (lib) wherein R ¹ , R ² , R ³ , R ⁴ , L ¹ , M ¹ , Q ¹ , Q ² , have the same meaning as that defined in any one of statements 27-32, preferably wherein R ³ and R ⁴ are each independently Ce-waryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl. The process according to any one of statements 1-33, wherein catalyst component B comprises bridged metallocene of formula (He) wherein R ¹ , R ² , R ³ , R ⁴ , L ¹ , M ¹ , Q ¹ , Q ² , have the same meaning as that defined in any one of statements 27-32, preferably wherein R ³ and R ⁴ are each independently Ce- aryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Ci-ealkoxy, halogen, haloCi-ealkyl.

35. The process according to any one of statements 1-34, wherein catalyst component B comprises a bridged metallocene of formula (lid), or (He)

36. A catalyst composition as recited in any one of statements 1-35. 37. An olefin polymerization process, the process comprising: contacting a catalyst composition according to statement 36, with an olefin monomer, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing the monomer, and the optionally one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining a polyolefin. 38. The process according to any one of statements 1-35, 37, wherein the process is performed in the slurry phase or gas phase or liquid phase, preferably in the slurry phase.

39. The process according to any one of statements 1-35, 37-38, wherein the process is conducted in one or more batch reactors, slurry reactors, gas-phase reactors, solution reactors, high pressure reactors, tubular reactors, autoclave reactors, or a combination thereof.

40. The process according to any one of statements 1-35, 37-39, wherein the process is conducted in a single reaction zone.

41. The process according to any one of statements 1-35, 37-40, wherein the olefin monomer is ethylene, and the olefin comonomer comprises propylene, 1 -butene, 2-butene, 3-methyl- 1 -butene, isobutylene, 1 -pentene, 2-pentene, 3-methyl-l-pentene, 4-methyl-1 -pentene, 1- hexene, 2-hexene, 3-ethyl-1 -hexene, 1 -heptene, 2-heptene, 3-heptene, 1 -octene, 1- decene, styrene, or a mixture thereof.

42. The process according to statement 37, wherein the olefin monomer is propylene, and the olefin comonomer comprises ethylene, 1 -butene, 2-butene, 3-methyl-1 -butene, isobutylene, 1 -pentene, 2-pentene, 3-methyl-1 -pentene, 4-methyl-1 -pentene, 1 -hexene, 2- hexene, 3-ethyl-l-hexene, 1 -heptene, 2-heptene, 3-heptene, 1 -octene, 1 -decene, styrene, or a mixture thereof.

43. The process according to any one of statements 1-35, 37-41 , wherein the olefin monomer is ethylene, and comprises contacting ethylene and optionally the olefin comonomer with the catalyst composition; and obtaining an ethylene polymer having a molecular weight distribution M _w /M _n ranging from 2.5 to 6.5, preferably from 2.6 to 6.3, preferably from 2.7 to 6.2, with M _w being the weight-average molecular weight and M _n being the numberaverage molecular weight.

44. The process according to any one of statements 1-35, 37-41 , 43, wherein the olefin monomer is ethylene, and comprises contacting ethylene and optionally the olefin comonomer with the catalyst composition; and obtaining an ethylene polymer having a molecular weight distribution M _z /M _w of at most 6.5, with M _z being the z average molecular weight, preferably at most 6.0, preferably at most 5.5, preferably at least 1.5, preferably at least 2.0.

45. The process according to any one of statements 1-35, 37-41 , 43-44, wherein the olefin monomer is ethylene, and comprises contacting ethylene and optionally the olefin comonomer with the catalyst composition; and obtaining an ethylene polymer having a total comonomer content, for example 1 -hexene content, relative to the total weight of the ethylene polymer ranging from 0.0 % by weight to 12.0 % by weight, as determined by ¹³ C NMR analysis, preferably from 0.0% by weight to 10.0 % by weight, preferably from 0.0% by weight to 9.0 % by weight.

46. The process according to any one of statements 1-35, 37-41 , 43-45, wherein the olefin monomer is ethylene, and comprises contacting ethylene and optionally the olefin comonomer with the catalyst composition; and obtaining an ethylene polymer having a melt index ranging from HLMI of 0.1 g/10 min to a melt index MI2 of 15.0 g/10 min wherein MI2 is determined according to ISO 1133:2005 Method B, condition D, at a temperature 190 °C, and a 2.16 kg load using a die of 2.096 mm, and high load melt flow index (HLMI) was determined according to ISO 1133:2005 Method B, condition G, at a temperature of 190 °C, and a 21.6 kg load using a die of 2.096 mm.

47. An olefin polymer at least partially catalyzed by at least one catalyst composition according to statement 36.

48. The olefin polymer according to statement 47, wherein said olefin polymer is an ethylene polymer.

49. The olefin polymer according to statement 48, having a melt index ranging from HLMI of 0.1 g/10 min to a melt index MI2 of 15.0 g/10 min wherein MI2 is determined according to ISO 1133:2005 Method B, condition D, at a temperature 190 °C, and a 2.16 kg load using a die of 2.096 mm, and high load melt flow index (HLMI) was determined according to ISO 1133:2005 Method B, condition G, at a temperature of 190 °C, and a 21.6 kg load using a die of 2.096 mm.

50. The olefin polymer according to any one of statements 48-49, having a molecular weight distribution M _w /M _n ranging from 2.5 to 6.5, preferably from 2.6 to 6.3, preferably from 2.7 to 6.2, with M _w being the weight-average molecular weight and M _n being the numberaverage molecular weight.

51. The olefin polymer according to any one of statements 48-50, having a molecular weight distribution M _z /M _w of at most 6.5, with M _z being the z average molecular weight, preferably at most 6.0, preferably at most 5.5, preferably at least 1 .5, preferably at least 2.0.

52. The olefin polymer according to any one of statements 48-51 , wherein said polymer is a homopolymer.

53. The olefin polymer according to any one of statements 48-52, wherein said polymer is a copolymer of ethylene and a higher alpha-olefin co-monomer, preferably 1 -hexene.

54. The olefin polymer according to any one of statements 48-53, having a total comonomer content, for example 1 -hexene content, relative to the total weight of the ethylene polymer ranging from 0.0 % by weight to 12.0 % by weight, as determined by ¹³ C NMR analysis, preferably from 0.0% by weight to 10.0 % by weight, preferably from 0.0% by weight to 9.0 % by weight.

55. The olefin polymer according to any one of statements 48-54, having a melt index ranging from HLMI of 0.10 g/10 min to a melt index MI2 of 15.0 g/10 min wherein MI2 is determined according to ISO 1133:2005 Method B, condition D, at a temperature 190 °C, and a 2.16 kg load using a die of 2.096 mm, and high load melt flow index (HLMI) was determined according to ISO 1133:2005 Method B, condition G, at a temperature of 190 °C, and a 21.6 kg load using a die of 2.096 mm; a molecular weight distribution M _w /M _n ranging from 2.5 to 6.5, preferably from 2.6 to 6.3, preferably from 2.7 to 6.2, with M _w being the weight-average molecular weight and M _n being the number-average molecular weight; a molecular weight distribution M _z /M _w of at most 6.5, with M _z being the z average molecular weight, preferably at most 6.0, preferably at most 5.5, preferably at least 1 .5, preferably at least 2.0; and a total comonomer content, for example 1 -hexene content, relative to the total weight of the ethylene polymer ranging from 0.0 % by weight to 12.0 % by weight, as determined by ¹³ C NMR analysis, preferably from 0.0% by weight to 10.0 % by weight, preferably from 0.0% by weight to 9.0 % by weight. An ethylene olefin polymer prepared according to a process according to any one of statements 1-35, 37-46. A metallocene-catalyzed ethylene polymer having a molecular weight distribution M _w /M _n ranging from 2.5 to 6.5, preferably from 2.6 to 6.3, preferably from 2.7 to 6.2, with M _w being the weight-average molecular weight and M _n being the number-average molecular weight. The metallocene-catalyzed ethylene polymer according to statement 57, having a molecular weight distribution M _z /M _w of at most 6.5, with M _z being the z average molecular weight, preferably at most 6.0, preferably at most 5.5, preferably at least 1 .5, preferably at least 2.0. The metallocene-catalyzed ethylene polymer according to any one of statements 57-58, having a melt index ranging from HLMI of 0.1 g/10 min to a melt index MI2 of 15.0 g/10 min wherein MI2 is determined according to ISO 1133:2005 Method B, condition D, at a temperature 190 °C, and a 2.16 kg load using a die of 2.096 mm, and high load melt flow index (HLMI) was determined according to ISO 1133:2005 Method B, condition G, at a temperature of 190 °C, and a 21.6 kg load using a die of 2.096 mm. The metallocene-catalyzed ethylene polymer according to any one of statements 57-59, wherein said polymer is a homopolymer. The metallocene-catalyzed ethylene polymer according to any one of statements 57-59, wherein said polymer is a copolymer of ethylene and a higher alpha-olefin co-monomer, preferably 1 -hexene. The metallocene-catalyzed ethylene polymer according to any one of statements 57-61 , having a total comonomer content, for example 1 -hexene content, relative to the total weight of the ethylene polymer ranging from 0.0 % by weight to 12.0 % by weight, as determined by ¹³ C NMR analysis, preferably from 0.0% by weight to 10.0 % by weight, preferably from 0.0% by weight to 9.0 % by weight. The metallocene-catalyzed ethylene polymer according to any one of statements 57-62, having a melt index ranging from HLMI of 0.10 g/10 min to a melt index MI2 of 15.0 g/10 min wherein MI2 is determined according to ISO 1133:2005 Method B, condition D, at a temperature 190 °C, and a 2.16 kg load using a die of 2.096 mm, and high load melt flow index (HLMI) was determined according to ISO 1133:2005 Method B, condition G, at a temperature of 190 °C, and a 21.6 kg load using a die of 2.096 mm; a molecular weight distribution M _w /M _n ranging from 2.5 to 6.5, preferably from 2.6 to 6.3, preferably from 2.7 to 6.2, with M _w being the weight-average molecular weight and M _n being the number-average molecular weight; a molecular weight distribution M _z /M _w of at most 6.5, with M _z being the z average molecular weight, preferably at most 6.0, preferably at most 5.5, preferably at least 1 .5, preferably at least 2.0; and a total comonomer content, for example 1 -hexene content, relative to the total weight of the ethylene polymer ranging from 0.0 % by weight to 12.0 % by weight, as determined by ¹³ C NMR analysis, preferably from 0.0% by weight to 10.0 % by weight, preferably from 0.0% by weight to 9.0 % by weight. The metallocene-catalyzed ethylene polymer according to any one of statements 57-63, wherein said metallocene is a metallocene catalyst composition according to statement 36. The metallocene-catalyzed ethylene polymer according to any one of statements 57-64, wherein said metallocene is a metallocene catalyst composition comprising: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; and wherein the unsubstituted or substituted aryl or heteroaryl is not on position 3 and/or 5 of each indenyl, preferably not on position 3 and 5 of each indenyl; preferably each indenyl has one or more substituents on positions 2 and/or 4 of each indenyl, preferably each indenyl has one substituent on position 2, preferably each indenyl has one substituent on position 4, yet more preferably each indenyl has one substituent on positions 2 and one substituent on position 4 of each indenyl, preferably the unsubstituted or substituted aryl or heteroaryl is on position 4 of each indenyl; and an optional activator; an optional support; and an optional co-catalyst. The metallocene-catalyzed ethylene polymer according to any one of statements 57-64, wherein said metallocene is a metallocene catalyst composition comprising: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups, each indenyl being independently substituted with two or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; each indenyl having at least one substituent on positions 2 and/or 4 of each indenyl, preferably each indenyl has one substituent on position 2, preferably each indenyl has one substituent on position 4, yet more preferably each indenyl has one substituent on positions 2 and one substituent on position 4 of each indenyl, preferably said unsubstituted or substituted aryl substituent on position 4 of each indenyl; and an optional activator; an optional support; and an optional co-catalyst. The metallocene-catalyzed ethylene polymer according to any one of statements 57-64, wherein said metallocene is a metallocene catalyst composition comprising: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups, each indenyl being independently substituted with two or more substituents, wherein one of the substituents is on position 2 of each indenyl and one other substituent is on position 4 of each indenyl, preferably wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; preferably wherein the unsubstituted or substituted aryl or heteroaryl is on the 4-position of each indenyl; preferably wherein the other substituents are not on position 3 and/or 5 of the indenyl; and an optional activator; an optional support; and an optional co-catalyst. The metallocene-catalyzed ethylene polymer according to any one of statements 57-64, wherein said metallocene is a metallocene catalyst composition comprising: catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; wherein the unsubstituted or substituted aryl or heteroaryl is on position 4 of each indenyl; and an optional activator; an optional support; and an optional co-catalyst. The metallocene-catalyzed ethylene polymer according to any one of statements 65-68, wherein the weight ratio of catalyst component A to catalyst component B is in a range of from 10/90 to 90/10, preferably in the range of from 20/80 to 80/20, preferably in the range of from 30/70 to 70/30, preferably in the range of from 40/60 to 60/40, preferably in the range of from 45/55 to 55/45.

70. The metallocene-catalyzed ethylene polymer according to any one of statements 65-69, wherein the bridged metallocene compound of catalyst component A comprises at least one alkenyl, cycloalkenyl, or cycloalkenylalkyl substituent, preferably at least one C3- 2oalkenyl, Cs-2ocycloalkenyl, or C6-2ocycloalkenylalkyl substituent, more preferably at least one Cs-salkenyl, Cs-scycloalkenyl, or Ce-scycloalkenylalkyl substituent.

71. The metallocene-catalyzed ethylene polymer according to any one of statements 65-70, wherein the bridged metallocene compound of catalyst component A comprises at least one alkenyl, cycloalkenyl, or cycloalkenylalkyl substituent on the bridge; preferably at least one C3-2oalkenyl, Cs-2ocycloalkenyl, or C6-2ocycloalkenylalkyl substituent, more preferably at least one Cs-salkenyl, Cs-scycloalkenyl, or Cs-scycloalkenylalkyl substituent.

72. The metallocene-catalyzed ethylene polymer according to any one of statements 65-71 , wherein catalyst component B contains a Si, or C bridging atom, optionally substituted with a one or two substituents each independently selected from alkyl, alkenyl, cycloalkyl, or cycloalkenyl.

73. The metallocene-catalyzed ethylene polymer according to any one of statements 65-72, wherein catalyst component A contains a C, Si, B or Ge bridging atom.

74. The metallocene-catalyzed ethylene polymer according to any one of statements 65-73, wherein the activator is methyl alumoxane.

75. The metallocene-catalyzed ethylene polymer according to any one of statements 65-74, wherein the catalyst composition comprises an organoaluminum co-catalyst.

76. The metallocene-catalyzed ethylene polymer according to any one of statements 65-75, comprising an alumoxane activator; and a titanated silica or silica solid support; and an optional co-catalyst.

77. The metallocene-catalyzed ethylene polymer according to any one of statements 65-76, wherein catalyst component A comprises a bridged metallocene of formula (I), wherein each of R ⁵ , R ⁶ , and R ⁷ , are independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each R ¹⁰ is independently hydrogen, alkyl, or alkenyl; and r, s, t are each independently an integer selected from 0, 1 , 2, 3, or 4;

L ² is -[CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, aminoalkyl, and arylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a cycloalkyl, cycloalkenyl or heterocyclyl;

M ² is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably is zirconium; and

Q ³ and Q ⁴ are each independently selected from the group comprising halogen, alkyl, - N(R ¹¹ ) ₂ , alkoxy, cycloalkoxy, aralkoxy, cycloalkyl, aryl, alkylaryl, aralkyl, and heteroalkyl; wherein R ¹¹ is hydrogen or alkyl. The metallocene-catalyzed ethylene polymer according to any one of statements 65-77, wherein catalyst component A comprises a bridged metallocene of formula (I), wherein each of R ⁵ , R ⁶ , and R ⁷ , are independently selected from the group consisting of Ci-2oalkyl, C3-2oalkenyl, C3-2ocycloalkyl, Cs-2ocycloalkenyl, C6-2ocycloalkenylalkyl, Ce-2oaryl, Ci-2oalkoxy, C?-2oalkylaryl, C?-2oarylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-2oalkyl; wherein each R ¹⁰ is independently hydrogen, Ci-2oalkyl, or C3-2oalkenyl; and r, s, t are each independently an integer selected from 0, 1 , 2, 3, or 4; L ² is -[CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group consisting of hydrogen, Ci- 2oalkyl, C3-2oalkenyl, C3-20 cycloalkyl, Cs-2ocycloalkenyl, C6-2ocycloalkenylalkyl, Ce- aryl, aminoCi-ealkyl, and C?-C2oarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a C3-2ocycloalkyl, Cs-2ocycloalkenyl or heterocyclyl;

M ² is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably is zirconium; and

Q ³ and Q ⁴ are each independently selected from the group comprising halogen, Ci-2oalkyl , -N(R ¹¹ ) ₂ , Ci-2oalkoxy, C3-2ocycloalkoxy, C?-2oaralkoxy, C3-2ocycloalkyl, Ce-2oaryl, C7- 2oalkylaryl, C?-2oaralkyl, and heteroCi-2oalkyl; wherein R ¹¹ is hydrogen or Ci-2oalkyl. The metallocene-catalyzed ethylene polymer according to any one of statements 65-78, wherein catalyst component A comprises a bridged metallocene of formula (la), wherein R ⁵ , R ⁶ , R ⁷ , L ² , M ² , Q ³ , Q ⁴ , and r have the same meaning as that defined in the any one of the preceding statements. The metallocene-catalyzed ethylene polymer according to any one of statements 65-79, wherein catalyst component A comprises a bridged metallocene of formula (lb), wherein R ⁶ , R ⁷ , L ² , M ² , Q ³ , Q ⁴ , have the same meaning as that defined in any one of the preceding statements. The metallocene-catalyzed ethylene polymer according to any one of statements 65-80, wherein catalyst component A comprises a bridged metallocene of formula (Ic), wherein R ⁶ , R ⁷ , R ⁸ , R ⁹ , M ² , Q ³ , Q ⁴ , have the same meaning as that defined in any one of the preceding statements, preferably each R ⁶ and R ⁷ is Ci-salkyl. The metallocene-catalyzed ethylene polymer according to any one of statements 65-81 , wherein catalyst component A comprises a bridged metallocene of formula (Id), (Id). The metallocene-catalyzed ethylene polymer according to any one of statements 65-83, wherein catalyst component B comprises a bridged metallocene catalyst of formula (II), wherein each of R ¹ , and R ³ , are independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each of said group can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, alkoxy, halogen, haloalkyl; wherein at least one of R ¹ or R ³ is unsubstituted or substituted aryl, wherein each R ¹⁰ is independently hydrogen, alkyl, aryl, or alkenyl; and m, p, are each independently an integer selected from 0, 1 , 2, 3, or 4, wherein at least one of m or p is at least 1 ; each of R ² , and R ⁴ , are independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, cycloalkenyl, cycloalkenylalkyl, phenyl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each of said group can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, alkoxy, halogen, haloalkyl; wherein at least one of R ² or R ⁴ is unsubstituted or substituted aryl, wherein each R ¹⁰ is independently hydrogen, alkyl, aryl, or alkenyl; and n, q are each independently an integer selected from 0, 1 , 2, 3, or 4, wherein at least one of n or q is at least 1 ;

L ¹ is SiR ⁸ R ⁹ , -[CR ⁸ R ⁹ ]h-, GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, aminoalkyl, and arylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a cycloalkyl, cycloalkenyl or heterocyclyl;

M ¹ is a transition metal selected from the group comprising zirconium, titanium, hafnium, and vanadium; and preferably M is zirconium; and

Q ¹ and Q ² are each independently selected from the group comprising hydrogen, halogen, hydroxyl, alkyl, alkenyl, -N(R ¹¹ )2, -SR ¹¹ , alkoxy, cycloalkoxy, aralkoxy, cycloalkyl, aryl, aryloxy, alkylaryl, aralkyl, and heteroalkyl; wherein R ¹¹ is hydrogen, alkyl or aryl. The metallocene-catalyzed ethylene polymer according to any one of statements 65-83, wherein catalyst component B comprises a bridged metallocene of formula (Ila), wherein R ¹ , R ² , R ³ , R ⁴ , L ¹ , M ¹ , Q ¹ , Q ² , m and n have the same meaning as that defined in any one of the preceding statements, preferably wherein R ³ and R ⁴ are each independently Ce- aryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Ci-ealkoxy, halogen, haloCi- ealkyl. The metallocene-catalyzed ethylene polymer according to any one of statements 65-84, wherein catalyst component B comprises bridged metallocene of formula (lib)

wherein R ¹ , R ² , R ³ , R ⁴ , L ¹ , M ¹ , Q ¹ , Q ² , have the same meaning as that defined in any one of the preceding statements, preferably wherein R ³ and R ⁴ are each independently Ce-waryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Ci-ealkoxy, halogen, haloCi- ealkyl.

86. The metallocene-catalyzed ethylene polymer according to any one of statements 65-85, wherein catalyst component B comprises bridged metallocene of formula (He) wherein R ¹ , R ² , R ³ , R ⁴ , L ¹ , M ¹ , Q ¹ , Q ² , have the same meaning as that defined in any one of the preceding statements, preferably wherein R ³ and R ⁴ are each independently Ce- aryl which can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising Ci-ealkyl, Ci-ealkoxy, halogen, haloCi- ealkyl. 87. The metallocene-catalyzed ethylene polymer according to any one of statements 65-86, wherein catalyst component B comprises a bridged metallocene of formula (lid), or (He)

88. The metallocene-catalyzed ethylene polymer according to any one of statements 65-87, prepared using a process according to any one of statements 1-35, 37-46.

89. An article comprising the polymer according to any one of statements 47-88, or comprising the polymer obtained using a process according to any one of statements 1-35, 37-46.

90. The article according to statement 89, wherein the article is selected from the group comprising pressure/temperature resistant pipe, film product, caps and closure, liner, rotomoulded article, or grass yarn, etc.

91. Use of a polymer according to any one of statements 47-88, or obtained using a process according to any one of statements 1-35, 37-46, in pressure/temperature resistant pipes application, film application, caps and closures applications, liners application, rotomoulding applications, grass yarn applications, etc.

The present invention provides an ethylene polymerization process, the process comprising: contacting a catalyst composition with ethylene, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing said ethylene and the optional one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining a polyethylene, wherein the catalyst composition comprises catalyst component A comprising a bridged metallocene compound with a substituted or unsubstituted cyclopentadienyl group and a substituted or unsubstituted fluorenyl group; catalyst component B comprising a bridged metallocene compound with two indenyl groups each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; wherein the unsubstituted or substituted aryl or heteroaryl substituent is not on the position 3 and/or 5 of the indenyl, preferably not on position 3 and 5 of each indenyl; preferably each indenyl has one or more substituents on positions 2 and/or 4 of each indenyl, preferably each indenyl has one substituent on position 2, preferably each indenyl has one substituent on position 4, yet more preferably each indenyl has one substituent on positions 2 and one substituent on position 4 of each indenyl, preferably the unsubstituted or substituted aryl or heteroaryl is on position 4 of each indenyl; and an optional activator; an optional support; and an optional co-catalyst.

For nomenclature purposes, the following numbering scheme is used for indenyl. It should be noted that indenyl can be considered a cyclopentadienyl with a fused benzene ring. The structure below is drawn and named as an anion: indenyl.

As used herein, the term “catalyst” refers to a substance that causes a change in the rate of a reaction. In the present invention, it is especially applicable to catalysts suitable for a polymerization, preferably for the polymerization of olefins to polyolefins.

The term "metallocene catalyst" is used herein to describe any transition metal complexes comprising metal atoms bonded to one or more ligands. The metallocene catalysts are compounds of Group IV transition metals of the Periodic Table such as titanium, zirconium, hafnium, etc., and have a coordinated structure with a metal compound and ligands composed of one or two groups of cyclopentadienyl, indenyl, tetrahydroindenyl, fluorenyl or their derivatives. Metallocenes comprise a single metal site, which allows for more control of branching and molecular weight distribution of the polymer. Monomers are inserted between the metal and the growing chain of polymer.

In one embodiment, for catalyst A, the bridged metallocene catalyst can be represented by the of compound of formula (III), and for catalyst B by compound of formula (IV): wherein

L ² (Ar ² )(Ar ³ )M ² Q ³ Q ⁴ (III),

L ¹ (Ar ¹ ) ₂ M ¹ Q ¹ Q ² (IV),

Ar ² is cyclopentadienyl, optionally substituted with one or more substituents each independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkenyl, or cycloalkenylalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each R ¹⁰ is independently hydrogen, alkyl, or alkenyl;

Ar ³ is fluorenyl, optionally substituted with one or more substituents each independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkenyl, or cycloalkenylalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each R ¹⁰ is independently hydrogen, alkyl, or alkenyl; each Ar ¹ is independently indenyl, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; preferably wherein the unsubstituted or unsubstituted or substituted aryl or heteroaryl substituent is not on the position 3 and/or 5 of the indenyl, preferably wherein the unsubstituted or substituted aryl or heteroaryl is on the 4-position of each indenyl; preferably, one or more substituents of indenyl is independently selected from the group comprising alkyl, alkenyl, cycloalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each of said group can be unsubstituted or substituted with one or more substituents each independently selected from the group comprising alkyl, alkenyl, cycloalkyl, cycloalkylalkyl, alkoxy, halogen, haloalkyl; wherein each R ¹⁰ is independently hydrogen, alkyl, or alkenyl. Each indenyl is substituted in the same way or differently from one another at one or more positions of either of the fused rings. Each substituent can be independently chosen. Preferably, each Ar ¹ is indenyl, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted aryl or heteroaryl; preferably wherein the unsubstituted or substituted aryl or heteroaryl substituent is on the 4-position of each indenyl, wherein Ar ¹ can be further substituted with one or more substituents each independently selected from the group comprising alkyl, alkenyl, cycloalkyl, aryl, alkoxy, alkylaryl, arylalkyl, halogen, Si(R ¹⁰ )3, and heteroalkyl; wherein each R ¹⁰ is independently hydrogen, alkyl, or alkenyl; each of M ¹ and M ² is a transition metal selected from the group comprising zirconium, hafnium, titanium, and vanadium; and preferably each of M ¹ and M ² is zirconium;

Q ¹ and Q ² are each independently selected from the group comprising hydrogen, halogen, alkyl, -N(R ¹¹ ) ₂ , alkoxy, cycloalkoxy, aralkoxy, cycloalkyl, aryl, alkylaryl, aralkyl, and heteroalkyl; wherein R ¹¹ is hydrogen or alkyl;

Q ³ and Q ⁴ are each independently selected from the group comprising halogen, alkyl, -N(R ¹¹ ) ₂ , alkoxy, cycloalkoxy, aralkoxy, cycloalkyl, aryl, alkylaryl, aralkyl, and heteroalkyl; wherein R ¹¹ is hydrogen or alkyl;

L ¹ is a divalent group or moiety bridging the two Ar ¹ groups, preferably selected from SiR ⁸ R ⁹ , -[CR ⁸ R ⁹ ]h-, GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, aminoalkyl, and arylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a cycloalkyl, cycloalkenyl or heterocyclyl; preferably L ¹ is SiR ⁸ R ⁹ ;

L ² is a divalent group or moiety bridging Ar ² and Ar ³ groups, preferably selected from -[CR ⁸ R ⁹ ]h- , SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, alkyl, alkenyl, cycloalkyl, cycloalkenyl, cycloalkenylalkyl, aryl, aminoalkyl, and arylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a cycloalkyl, cycloalkenyl or heterocyclyl.

In some embodiments, each Ar ¹ is indenyl, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an aryl or heteroaryl; preferably wherein the aryl or heteroaryl substituent is on the 4-position of each indenyl; each indenyl being further optionally substituted with one or more substituents each independently selected from the group comprising Ci-2oalkyl, C3-2oalkenyl, C3-2ocycloalkyl, Cs-2ocycloalkenyl, C6-2ocycloalkenylalkyl, Ce-2oaryl, Ci-2oalkoxy, C?-2oalkylaryl, C?-2oarylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-^alkyl (said further substituent being preferably on position 2 of each indenyl); wherein each R ¹⁰ is independently hydrogen, Ci-2oalkyl , or C3-2oalkenyl.

Preferably each Ar ¹ is indenyl, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted Ce- waryl; wherein the unsubstituted or substituted Ce-waryl is on the 4-position on each indenyl; each indenyl being further substituted on position 2 with one or more substituents each independently selected from the group comprising Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Cs- scycloalkenyl, Ce-scycloalkenylalkyl, Ce- aryl, Ci-salkoxy, Cy-walkylaryl, Cy-warylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-salkyl; wherein each R ¹⁰ is independently hydrogen, Ci-salkyl, or Cs- salkenyl.

Preferably each Ar ¹ is indenyl, each indenyl being independently substituted with one or more substituents, wherein at least one of the substituents is an unsubstituted or substituted Ce- waryl; preferably wherein the unsubstituted or substituted Ce-waryl is on the 4-position on each indenyl; each indenyl being further optionally substituted on position 2 with a substituent independently selected from the group comprising Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Ce- waryl, and halogen.

In some embodiments, Ar ² is cyclopentadienyl, optionally substituted with one or more substituents each independently selected from the group comprising Ci-2oalkyl, C3-2oalkenyl, C3-2ocycloalkyl, Cs-2ocycloalkenyl, Ce-2ocycloalkenylalkyl, Ce-2oaryl, Ci-2oalkoxy, Cy-2oalkylaryl, Cy-2oarylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-walkyl; wherein each R ¹⁰ is independently hydrogen, Ci-2oalkyl, or C3-2oalkenyl. Preferably Ar ² is cyclopentadienyl, optionally substituted with one or more substituents each independently selected from the group comprising Ci- salkyl, Cs-salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Ce-scycloalkenylalkyl, Ce-waryl, Ci-salkoxy, C?-i2alkylaryl, Cy-warylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-salkyl; wherein each R ¹⁰ is independently hydrogen, Ci-salkyl, or Cs-salkenyl. Preferably Ar ² is cyclopentadienyl, optionally substituted with one or more substituents each independently selected from the group comprising Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Ce-waryl, and halogen.

In some embodiments, Ar ³ is fluorenyl, optionally substituted with one or more substituents each independently selected from the group comprising Ci-2oalkyl, C3-2oalkenyl, C3-2ocycloalkyl, Cs-2ocycloalkenyl, C6-2ocycloalkenylalkyl, Cs-2oaryl, Ci-2oalkoxy, C?-2oalkylaryl, C?-2oarylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-^alkyl; wherein each R ¹⁰ is independently hydrogen, Ci-2oalkyl , or C3-2oalkenyl. Preferably Ar ² is fluorenyl, optionally substituted with one or more substituents each independently selected from the group comprising Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Cs-scycloalkenylalkyl, Ce-waryl, Ci-salkoxy, C?-i2alkylaryl, C?-i2arylalkyl, halogen, Si(R ¹⁰ )3, and heteroCi-salkyl; wherein each R ¹⁰ is independently hydrogen, Ci-salkyl, or Cs-salkenyl. Preferably, Ar ³ is fluorenyl, optionally substituted with one or more substituents each independently selected from the group comprising Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Ce- aryl, and halogen.

In some embodiments, L ¹ is -[CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-2oalkyl, Cs-2oalkenyl, Cs-2ocycloalkyl, Cs-2ocycloalkenyl, Ce- 2ocycloalkenylalkyl, Ce-waryl, and Cy-Csoarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a Cs-2ocycloalkyl, Cs-2ocycloalkenyl or heterocyclyl. Preferably L ¹ is - [CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-salkyl, Cs- salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Cs-scycloalkenylalkyl, Ce-waryl, and Cy-Cwarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a Cs-scycloalkyl, Cs- scycloalkenyl or heterocyclyl. Preferably, L ¹ is -[CR ⁸ R ⁹ ]h-, or SiR ⁸ R ⁹ ; wherein h is an integer selected from 1 , or 2; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Cs-scycloalkenylalkyl, and Ce- waryl. Preferably, L ¹ is SiR ⁸ R ⁹ ; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Ce- scycloalkenylalkyl, and Ce-waryl; preferably Ci-salkyl.

In some embodiments, Q ¹ and Q ² are each independently selected from the group comprising hydrogen, halogen, Ci-2oalkyl, -N(R ¹¹ )2, Ci-2oalkoxy, Cs-2ocycloalkoxy, C?-2oaralkoxy, C3- 2ocycloalkyl, Ce-2oaryl, C?-2oalkylaryl, C?-2oaralkyl, and heteroCi-2oalkyl; wherein R ¹¹ is hydrogen or Ci-2oalkyl. Preferably Q ¹ and Q ² are each independently selected from the group comprising halogen, Ci-salkyl, -N(R ¹¹ )2, Ci-salkoxy, Cs-scycloalkoxy, Cy-waralkoxy, Cs-scycloalkyl, Ce-waryl, C?-i2alkylaryl, Cy-waralkyl, and heteroCi-salkyl; wherein R ¹¹ is hydrogen or Ci-salkyl. Preferably, Q ¹ and Q ² are each independently selected from the group comprising halogen, Ci-salkyl, - N(R ¹¹ ) ₂ , Ce-waryl, and Cy-waralkyl; wherein R ¹¹ is hydrogen or Ci-salkyl, preferably Q ¹ and Q ² are each independently selected from the group comprising Cl, F, Br, I, methyl, benzyl, and phenyl.

In some embodiments, L ² is -[CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-2oalkyl, C3-2oalkenyl, C3-2ocycloalkyl, Cs-2ocycloalkenyl, Ce- 2ocycloalkenylalkyl, Cs- aryl, and Cy-C2oarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a C3-2ocycloalkyl, Cs-2ocycloalkenyl or heterocyclyl. Preferably L ² is - [CR ⁸ R ⁹ ]h-, SiR ⁸ R ⁹ , GeR ⁸ R ⁹ , or BR ⁸ ; wherein h is an integer selected from 1 , 2, or 3; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-salkyl, C3- salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Ce-scycloalkenylalkyl, Ce- aryl, and Cy-Cwarylalkyl; or R ⁸ and R ⁹ together with the atom to which they are attached form a Cs-scycloalkyl, C5- scycloalkenyl or heterocyclyl. Preferably, L ² is -[CR ⁸ R ⁹ ]h-, or SiR ⁸ R ⁹ ; wherein h is an integer selected from 1 , or 2; each of R ⁸ , and R ⁹ are independently selected from the group comprising hydrogen, Ci-salkyl, Cs-salkenyl, Cs-scycloalkyl, Cs-scycloalkenyl, Ce-scycloalkenylalkyl, and Ce- waryl.

In some embodiments, Q ³ and Q ⁴ are each independently selected from the group comprising hydrogen, halogen, Ci-2oalkyl, -N(R ¹¹ )2, Ci-2oalkoxy, C3-2ocycloalkoxy, C?-2oaralkoxy, C3- 2ocycloalkyl, Ce-2oaryl, C?-2oalkylaryl, C?-2oaralkyl, and heteroCi-2oalkyl; wherein R ¹¹ is hydrogen or Ci-2oalkyl. Preferably Q ³ and Q ⁴ are each independently selected from the group comprising halogen, Ci-salkyl, -N(R ¹¹ )2, Ci-salkoxy, Cs-scycloalkoxy, Cy-waralkoxy, Cs-scycloalkyl, Ce-waryl, C?-i2alkylaryl, Cy-waralkyl, and heteroCi-salkyl; wherein R ¹¹ is hydrogen or Ci-salkyl. Preferably, Q ³ and Q ⁴ are each independently selected from the group comprising halogen, Ci-salkyl, - N(R ¹¹ ) ₂ , Ce-waryl, and Cy-waralkyl; wherein R ¹¹ is hydrogen or Ci-salkyl, preferably Q ¹ and Q ² are each independently selected from the group comprising Cl, F, Br, I, methyl, benzyl, and phenyl.

In some preferred embodiments, catalyst component A comprises a bridged metallocene catalyst of formula (I), wherein each of R ⁵ , R ⁶ , R ⁷ , r, s, t, L ² , M ² , Q ³ and Q ⁴ have the same meaning as that defined herein above and in the statements.

In some preferred embodiments, catalyst component A comprises a bridged metallocene catalyst of formula (la), wherein each of R ⁵ , R ⁶ , R ⁷ , r, L ² , M ² , Q ³ and Q ⁴ have the same meaning as that defined herein above and in the statements.

Non-limiting examples of catalyst A are shown below:

In some preferred embodiments, catalyst component B comprises a bridged metallocene

5 catalyst of formula (II); wherein wherein each of R ¹ , R ² , R ³ and R ⁴ , m, n, p, q, L ¹ , M ¹ , Q ¹ and Q ² have the same meaning as that defined herein above and in the statements.

In some preferred embodiments, catalyst component B comprises a bridged metallocene catalyst of formula (lib) or (lie) wherein R ¹ , R ² , R ³ , R ⁴ , L ¹ , M ¹ , Q ¹ , Q ² , have the same meaning as that defined herein above and in the statements.

Non-limiting examples of catalyst B are shown below:

In a preferred embodiment, the weight ratio of catalyst component A to catalyst component B is in a range of from 10/90 to 90/10, preferably in the range of from 15/85 to 85/15, preferably in the range of from 25/75 to 75/25, preferably in the range of from 35/65 to 65/35, preferably in the range of from 45/55 to 55/45. The catalyst components A and B herein are preferably provided on a solid support, preferably both catalysts are provided on a single solid support, thereby forming a dual catalyst system.

The support can be an inert organic or inorganic solid, which is chemically unreactive with any of the components of the conventional bridged metallocene catalyst. Suitable support materials for the supported catalyst include solid inorganic oxides, such as silica, alumina, magnesium oxide, titanium oxide, thorium oxide, as well as mixed oxides of silica and one or more Group 2 or 13 metal oxides, such as silica-magnesia and silica-alumina mixed oxides. Silica, alumina, and mixed oxides of silica and one or more Group 2 or 13 metal oxides are preferred support materials. Preferred examples of such mixed oxides are the silica-aluminas. For example the solid oxide comprises titanated silica, silica, alumina, silica-alumina, silica-coated alumina, aluminum phosphate, aluminophosphate, heteropolytungstate, titania, zirconia, magnesia, boria, zinc oxide, a mixed oxide thereof, or any mixture thereof, preferably silica, titanated silica, silica treated with fluoride, silica-alumina, alumina treated with fluoride, sulfated alumina, silica-alumina treated with fluoride, sulfated silica-alumina, silica-coated alumina, silica treated with fluoride, sulfated silica-coated alumina, or any combination thereof. Most preferred is a titanated silica, or a silica compound. In a preferred embodiment, the bridged metallocene catalysts are provided on a solid support, preferably a titanated silica, or a silica support. The silica may be in granular, agglomerated, fumed or other form.

In some embodiments, the support of catalyst components A and B is a porous support, and preferably a porous titanated silica, or silica support having a surface area comprised between 200 and 900 m ² /g. In another embodiment, the support of the polymerization catalyst is a porous support, and preferably a porous titanated silica, or silica support having an average pore volume comprised between 0.5 and 4 mL/g. In yet another embodiment, the support of the polymerization catalyst is a porous support, and preferably a porous titanated silica, or silica support having an average pore diameter comprised between 50 and 300 A, and preferably between 75 and 220 A.

In some embodiments, the support has a D50 of at most 150 pm, preferably of at most 100 pm, preferably of at most 75 pm, preferably of at most 50 pm, preferably of at most 40 pm, preferably of at most 30 pm. The D50 is defined as the particle size for which fifty percent by weight of the particles has a size lower than the D50. The measurement of the particle size can be made according to the International Standard ISO 13320:2009 ("Particle size analysis -Laser diffraction methods"). For example, the D50 can be measured by sieving, by BET surface measurement, or by laser diffraction analysis. For example, Malvern Instruments' laser diffraction systems may advantageously be used. The particle size may be measured by laser diffraction analysis on a Malvern type analyzer. The particle size may be measured by laser diffraction analysis on a Malvern type analyzer after having put the supported catalyst in suspension in cyclohexane. Suitable Malvern systems include the Malvern 2000, Malvern MasterSizer (such as Mastersizer S), Malvern 2600 and Malvern 3600 series. Such instruments together with their operating manual meet or even exceed the requirements set- out within the ISO 13320 Standard. The Malvern MasterSizer (such as Mastersizer S) may also be useful as it can more accurately measure the D50 towards the lower end of the range e.g., for average particle sizes of less 8 pm, by applying the theory of Mie, using appropriate optical means.

Preferably, catalyst components A and B are activated by an activator. The activator can be any activator known for this purpose such as an aluminum-containing activator, a boron- containing activator, or a fluorinated activator. The aluminum-containing activator may comprise an alumoxane, an alkyl aluminum, a Lewis acid and/or a fluorinated catalytic support.

In some embodiments, alumoxane is used as an activator for catalyst components A and B. The alumoxane can be used in conjunction with a catalyst in order to improve the activity of the catalyst during the polymerization reaction.

As used herein, the term “alumoxane” and “aluminoxane” are used interchangeably, and refer to a substance, which is capable of activating the bridged metallocene catalyst. In some embodiments, alumoxanes comprise oligomeric linear and/or cyclic alkyl alumoxanes. In a further embodiment, the alumoxane has formula (V) or (VI)

R ^a -(AI(R ^a )-O) _x -AIR ^a 2 (V) for oligomeric, linear alumoxanes; or

(-AI(R ^a )-O-) _y (VI) for oligomeric, cyclic alumoxanes wherein x is 1-40, and preferably 10-20; wherein y is 3-40, and preferably 3-20; and wherein each R ^a is independently selected from a Ci-salkyl, and preferably is methyl. In a preferred embodiment, the alumoxane is methylalumoxane (MAO).

The catalyst composition may comprise a co-catalyst. One or more aluminumalkyl represented by the formula AIR ^b _x can be used as additional co-catalyst, wherein each R ^b is the same or different and is selected from halogens or from alkoxy or alkyl groups having from 1 to 12 carbon atoms and x is from 1 to 3. Non-limiting examples are Tri-Ethyl Aluminum (TEAL), Tri- Iso-Butyl Aluminum (TIBAL), Tri-Methyl Aluminum (TMA), and Methyl-Methyl-Ethyl Aluminum (MMEAL). Especially suitable are trialkylaluminums, the most preferred being triisobutylaluminum (TIBAL) and triethylaluminum (TEAL).

The present invention also encompasses a catalyst composition as defined herein (including all embodiments thereof as described herein).

The catalyst composition can be particularly useful in a process for the preparation of a polymer comprising contacting at least one monomer with at least one catalyst composition. Preferably, said polymer is a polyolefin, preferably said monomer is an alpha-olefin.

The catalyst composition of the present invention is therefore particularly suitable for being used in the preparation of a polyolefin. The present invention also relates to the use of a catalyst composition in olefin polymerization.

The present invention also encompasses an olefin polymerization process, the process comprising: contacting a catalyst composition according to the invention, with an olefin monomer, optionally hydrogen, and optionally one or more olefin comonomers; and polymerizing the monomer, and the optionally one or more olefin comonomers, in the presence of the at least one catalyst composition, and optional hydrogen, thereby obtaining a polyolefin.

The term “olefin” refers herein to molecules composed of carbon and hydrogen, containing at least one carbon-carbon double bond. Olefins containing one carbon-carbon double bond are denoted herein as mono-unsaturated hydrocarbons and have the chemical formula C _n H2n, where n equals at least two. “Alpha-olefins”, “a-olefins”, “1 -alkenes” or “terminal olefins” are used as synonyms herein and denote olefins or alkenes having a double bond at the primary or alpha (a) position.

Throughout the present application the terms “olefin polymer”, "polyolefin" and "polyolefin polymer" may be used synonymously.

Suitable polymerization includes but is not limited to homopolymerization of an alpha-olefin, or copolymerization of the alpha-olefin and at least one other alpha-olefin comonomer.

As used herein, the term “comonomer” refers to olefin comonomers which are suitable for being polymerized with alpha-olefin monomer. The comonomer if present is different from the olefin monomer and chosen such that it is suited for copolymerization with the olefin monomer. Comonomers may comprise but are not limited to aliphatic C2-C20 alpha-olefins. Examples of suitable aliphatic C3-C20 alpha-olefins include ethylene, propylene, 1 -butene, 1 -pentene, 4- methyl-1 -pentene, 1 -hexene, 1 -octene, 1 -decene, 1 -dodecene, 1 -tetradecene, 1 -hexadecene, 1 -octadecene, and 1-eicosene. Further examples of suitable comonomers are vinyl acetate (H3C-C(=O)O-CH=CH2) or vinyl alcohol ("HO-CH=CH2"). Examples of olefin copolymers suited which can be prepared can be random copolymers of propylene and ethylene, random copolymers of propylene and 1 -butene, heterophasic copolymers of propylene and ethylene, ethylene-butene copolymers, ethylene-hexene copolymers, ethylene-octene copolymers, copolymers of ethylene and vinyl acetate (EVA), copolymers of ethylene and vinyl alcohol (EVOH).

In some embodiments, the olefin monomer is ethylene, and the olefin comonomer comprises propylene, 1 -butene, 2-butene, 3-methyl-1 -butene, isobutylene, 1 -pentene, 2-pentene, 3- methyl-l-pentene, 4-methyl-1 -pentene, 1 -hexene, 2-hexene, 3-ethyl-1 -hexene, 1 -heptene, 2- heptene, 3-heptene, 1-octene, 1-decene, styrene, or a mixture thereof.

In some embodiments, the olefin monomer is propylene, and the olefin comonomer comprises ethylene, 1 -butene, 2-butene, 3-methyl-1 -butene, isobutylene, 1 -pentene, 2-pentene, 3- methyl-1 -pentene, 4-methyl-1 -pentene, 1 -hexene, 2-hexene, 3-ethyl-l-hexene, 1 -heptene, 2- heptene, 3-heptene, 1-octene, 1-decene, styrene, or a mixture thereof.

The polyolefin can be prepared out in bulk, gas, solution and/or slurry phase. The process can be conducted in one or more batch reactors, slurry reactors, gas-phase reactors, solution reactors, high pressure reactors, tubular reactors, autoclave reactors, or a combination thereof.

The polymerization can be carried out batchwise or in a continuous process.

The term "slurry" or "polymerization slurry" or "polymer slurry", as used herein refers to substantially a multi-phase composition including at least polymer solids and a liquid phase, the liquid phase being the continuous phase. The solids may include the catalyst and polymerized monomer.

In some embodiments, the liquid phase comprises a diluent. As used herein, the term “diluent” refers to any organic diluent, which does not dissolve the synthesized polyolefin. As used herein, the term “diluent” refers to diluents in a liquid state, liquid at room temperature and preferably liquid under the pressure conditions in the loop reactor. Suitable diluents comprise but are not limited to hydrocarbon diluents such as aliphatic, cycloaliphatic and aromatic hydrocarbon solvents, or halogenated versions of such solvents. Preferred solvents are C12 or lower, straight chain or branched chain, saturated hydrocarbons, C5 to C9 saturated alicyclic or aromatic hydrocarbons or C2 to Ce halogenated hydrocarbons. Non-limiting illustrative examples of solvents are butane, isobutane, pentane, hexane, heptane, cyclopentane, cyclohexane, cycloheptane, methyl cyclopentane, methyl cyclohexane, isooctane, benzene, toluene, xylene, chloroform, chlorobenzenes, tetrachloroethylene, dichloroethane and trichloroethane, preferably isobutane or hexane.

The polymerization can also be performed in gas phase, under gas phase conditions. The term "gas phase conditions" as used herein refers to temperatures and pressures suitable for polymerizing one or more gaseous phase olefins to produce polymer therefrom.

The polymerization steps can be performed over a wide temperature range. In certain embodiments, the polymerization steps may be performed at a temperature from 20 °C to 125 °C, preferably from 60 °C to 110 °C, more preferably from 75 °C to 100 °C and most preferably from 78 °C to 98 °C. Preferably, the temperature range may be within the range from 75 °C to 100 °C and most preferably from 78 °C to 98 °C. Said temperature may fall under the more general term of polymerization conditions. In certain embodiments, in slurry conditions, the polymerization steps may be performed at a pressure from about 20 bar to about 100 bar, preferably from about 30 bar to about 50 bar, and more preferably from about 37 bar to about 45 bar. Said pressure may fall under the more general term of polymerization conditions.

The invention also encompasses a polymer at least partially catalyzed by at least one composition according to the invention or produced by a process according to the invention.

The present invention also encompasses a polymer, preferably an olefin polymer produced by a process as defined herein. In some embodiments, said olefin polymer is polyethylene. In some embodiments, said olefin polymer is polypropylene.

The term “polyolefin resin” or “polyolefin” as used herein refers to the polyolefin fluff or powder that is extruded, and/or melted, and/or pelleted and can be prepared through compounding and homogenizing of the polyolefin resin as taught herein, for instance, with mixing and/or extruder equipment.

The term “ethylene polymer”, “polyethylene resin” or “polyethylene” as used herein refers to the ethylene polymer fluff or powder that is extruded, and/or melted, and/or pelleted and can be prepared through compounding and homogenizing of the ethylene polymer as taught herein, for instance, with mixing and/or extruder equipment. Unless otherwise stated, all parameters used to define the polyethylene resin, are as measured on ethylene polymer pellets.

The term “fluff” or “powder” as used herein refers to the polyolefin material with the solid catalyst particle at the core of each grain and is defined as the polymer material after it exits the polymerization reactor (or final polymerization reactor in the case of multiple reactors connected in series). The term “pellets” refers to the polyolefin fluff that has been pelletized, for example through melt extrusion. As used herein, the terms “extrusion” or “extrusion process”, “pelletization” or “pelletizing” are used herein as synonyms and refer to the process of transforming polyolefin resin into a “polyolefin product” or into “pellets” after pelletizing. The process of pelletization preferably comprises several devices connected in series, including one or more rotating screws in an extruder, a die, and means for cutting the extruded filaments into pellets.

In an embodiment, the olefin polymer is a homopolymer. The term “homopolymer” as used herein is intended to encompass polymers which consist essentially of repeat units deriving from the monomer. Homopolymers may, for example, comprise at least 99.8% preferably 99.9% by weight of repeats units derived from the monomer, as determined for example by ¹³ C NMR spectrometry.

In some embodiments, the olefin polymer is an ethylene polymer. In some embodiments, . The term “copolymer” as used herein is intended to encompass polymers which consist essentially of repeat units deriving from the monomer and at least one other C3-C20 alpha-olefin comonomer, preferably wherein the co-monomer is 1 -hexene.

As used herein, the term “co-monomer” refers to olefin co-monomers which are suitable for being polymerized with alpha-olefin monomer. Co-monomers may comprise but are not limited to aliphatic C3-C20 alpha-olefins, preferably C3-C12 alpha-olefins. Examples of suitable aliphatic C3-C20 alpha-olefins include propylene, 1 -butene, 1 -pentene, 4-methyl-1 -pentene, 1 -hexene, 1 -octene, 1 -decene, 1 -dodecene, 1 -tetradecene, 1 -hexadecene, 1 -octadecene, and 1- eicosene. In some preferred embodiments, said co-monomer is 1-hexene.

In some embodiments, the olefin polymer is an ethylene polymer. In some embodiments, said ethylene polymer is a copolymer of ethylene and a higher alpha-olefin co-monomer, preferably 1-hexene, wherein the total co-monomer content, preferably 1-hexene (wt.% C6-) relative to the total weight of the ethylene polymer is at least 0.5 % by weight, preferably at least 1.0 % by weight, preferably at least 1.5 % by weight, preferably at least 2.0 % by weight, preferably at least 2.5 % by weight, preferably at least 3.0 % by weight, as determined by ¹³ C NMR analysis. In some embodiments, said ethylene polymer is a copolymer of ethylene and a higher alpha-olefin co-monomer, preferably 1-hexene, wherein the total co-monomer content, preferably 1-hexene (wt.% C6-) relative to the total weight of the polyethylene is at most 12.0 % by weight, preferably at most 10.0 % by weight, preferably at most 9.0 % by weight, as determined by ¹³ C NMR analysis.

Ethylene copolymers described herein can, in some embodiments, have a non-conventional (reverse or inverse) co-monomer distribution, i.e. , the higher molecular weight portions of the polymer have higher co-monomer incorporation than the lower molecular weight portions. Preferably, there is an increasing co-monomer incorporation with increasing molecular weight, as shown by the ratio of the areas of IR signals (ACH3/ACH2) from IR5-MCT detector as function of log M.

As used herein, the term “monomodal ethylene polymer” or “ethylene polymer with a monomodal molecular weight distribution” refers to polyethylene having one maximum in their molecular weight distribution curve, which is also defined as a unimodal distribution curve. As used herein, the term “polyethylene with a bimodal molecular weight distribution” or “bimodal polyethylene” it is meant, polyethylene having a distribution curve being the sum of two unimodal molecular weight distribution curves, and refers to a polyethylene product having two distinct but possibly overlapping populations of polyethylene macromolecules each having different weight average molecular weights. By the term “polyethylenes with a multimodal molecular weight distribution” or “multimodal polyethylenes” it is meant polyethylenes with a distribution curve being the sum of at least two, preferably more than two unimodal distribution curves, and refers to a polyethylene product having two or more distinct but possibly overlapping populations of polyethylene macromolecules each having different weight average molecular weights. The multimodal polyethylene can have an “apparent monomodal” molecular weight distribution, which is a molecular weight distribution curve with a single peak and no shoulder. Nevertheless, the polyethylene will still be multimodal if it comprises two distinct populations of polyethylene macromolecules each having a different weight average molecular weights, as defined above, for example when the two distinct populations were prepared in different reactors and/or under different conditions and/or with different catalysts.

The present invention also encompasses a polyethylene composition comprising the ethylene polymer of the invention and one or more additives.

The additives can be for example antioxidants, UV stabilizers, pigments, processing aids, acid scavengers, lubricants, antistatic agents, fillers, nucleating agents, or clarifying agents, or combination thereof. An overview of useful additives is given in Plastics Additives Handbook, ed. H. Zweifel, 5 ^th edition, Hanser Publishers. These additives may be present in quantities generally between 0.01 and 10 weight % based on the weight of the polyethylene composition.

After the ethylene polymer is produced, it may be formed into various articles. The ethylene polymer is particularly suited for articles such as pressure/temperature resistant pipe, film product, caps and closure, liner, rotomoulded article, or grass yarn, etc.

The present invention therefore also encompasses an article comprising an ethylene polymer as defined herein; or obtained according to a process as defined herein. In some embodiments, said article can be pressure/temperature resistant pipe, film product, caps and closure, liner, rotomoulded article, or grass yarn, etc.

Preferred embodiments for ethylene polymer of the invention are also preferred embodiments for the article of the invention.

The invention also encompasses a process for preparing an article according to the invention. Preferred embodiments as described above are also preferred embodiments for the present process.

The following examples serve to merely illustrate the invention and should not be construed as limiting its scope in any way. While the invention has been shown in only some of its forms, it should be apparent to those skilled in the art that it is not so limited, but is susceptible to various changes and modifications without departing from the scope of the invention.

EXAMPLES

TEST METHODS

The properties cited herein and cited below were determined in accordance with the following test procedures. Where any of these properties is referenced in the appended claims, it is to be measured in accordance with the specified test procedure. Melt flow index

The melt flow index (MI2) of ethylene polymers was determined according to ISO 1133:2005 Method B, condition D, at a temperature of 190 °C, and a 2.16 kg load using a die of 2.096 mm.

The high load melt flow index (HLMI) of ethylene polymers was determined according to ISO 1133:2005 Method B, condition G, at a temperature of 190 °C, and a 21.6 kg load using a die of 2.096 mm.

Molecular weight, molecular distribution

The molecular weight (M _n (number average molecular weight), M _w (weight average molecular weight) and molecular weight distributions D (M _w /M _n ), and D’ (M _z /M _w ) were determined by size exclusion chromatography (SEC) and in particular by IR-detected gel permeation chromatography (GPC) at high temperature (145 °C). Briefly, a GPC-IR5MCT from Polymer Char was used: 8 mg polymer sample was dissolved at 160 °C in 8 mL of trichlorobenzene stabilized with 1000 ppm by weight of butylhydroxytoluene (BHT) for 1 hour (h). Injection volume: about 400 pl, automatic sample preparation and injection temperature: 160 °C. Column temperature: 145 °C. Detector temperature: 160 °C. Column set: two Shodex AT- 806MS (Showa Denko) and one Styragel HT6E (Waters), columns were used with a flow rate of 1 mL/min. Detector: Infrared detector (2800-3000 cm ^-1 ) to collect all C-H bonds and two narrow band filters tuned to the absorption region assigned to CH3 and CH2 groups. Calibration: narrow standards of polystyrene (PS) (commercially available). Calculation of molecular weight Mj of each fraction i of eluted polymer is based on the Mark-Houwink relation (log (MpE) = 0.965909 x log10(Mps) - 0.28264) (cut off on the low molecular weight end at M _PE = 1000).

The molecular weight averages used in establishing molecular weight/property relationships are the number average (M _n ), weight average (M _w ) and z average (M _z ) molecular weight. These averages are defined by the following expressions and are determined form the calculated Mi:

Here Nj and are the number and weight, respectively, of molecules having molecular weight Mj. The third representation in each case (farthest right) defines how one obtains these averages from SEC chromatograms, hi is the height (from baseline) of the SEC curve at the i _th elution fraction and Mj is the molecular weight of species eluting at this increment.

Comonomer content

The comonomer content, especially 1 -hexene, (wt.% C6-) relative to the total weight of the ethylene polymer was determined from a ¹³ C{ ¹ H} NMR spectrum. Ethyl branches content, expressed in terms of equivalent wt.% C4-, was also determined from a ¹³ C{ ¹ H} NMR spectrum.

The sample was prepared by dissolving a sufficient amount of polymer in 1 ,2,4- trichlorobenzene (TCB 99% spectroscopic grade) at 130 °C and occasional agitation to homogenize the sample, followed by the addition of hexadeuterobenzene (CeDe, spectroscopic grade) and a minor amount of hexamethyldisiloxane (HMDS, 99.5+%), with HMDS serving as internal standard. To give an example, about 220 mg of polymer were dissolved in 2.0 mL of TCB, followed by addition of 0.5 mL of CeDe and 2 to 3 drops of HMDS.

¹³ C{ ¹ H} NMR signal was recorded on a Bruker 500 MHz with a 10 mm probe (or 10 mm cryoprobe) with the following conditions:

Pulse angle: 90 °

Pulse repetition time: 30 s

Spectral width: 25000 Hz centered at 95 ppm

Data points: 64K

Temperature: 130 °C +1-2 °C

Rotation: 15 Hz

Scan numbers: 2000 - 4000 (240 scans with 10 mm cryoprobe)

Decoupling sequence: inverse-gated decoupling sequence to avoid NOE effect

¹³ C{ ¹ H} NMR spectrum was obtained by Fourier Transform on 131 K points after a light Gaussian multiplication. Spectrum was phased, baseline corrected, and chemical shift scale was referenced to the internal standard HMDS at 2.03 ppm.

Chemical shifts of signals were peak picked, and peaks were integrated as mentioned on Figure 1 and in the following Table A.

Table A: integration regions of ¹³ C{ ¹ H} NMR spectrum

Small adjustments on integration limits can be applied if necessary.

Chemical shifts are given at ± 0.05 ppm.

The wt.% C6- and wt.% C4- contents are obtained by the following areas (A) combinations:

AC3 = 0.5 X AcH2(a) B1 AC4 = ACH3 B2

AC6 - ACH2(2) B4

AC2 - 0.5 X (ATV1 + ATV2 + ATV3 + Avinylidenel + Avinylidene2 + 0.5 X AcH2(a) B1 + ATS3 + 2X ATS2 + AcH2n '

AC6 ⁺ AcH2(b) )

Comonomer distribution

Co-monomer distribution illustrated by the CH3/CH2 ratio across the molecular weight distribution was also determined using the SEC apparatus described above equipped with an integrated high-sensitivity multiple band IR detector (IR5-MCT) as described by A. Ortin et al. (Macromol. Symp. 330, 63-80 2013 and T. Frijns-Bruls et al. Macromol. Symp. 356, 87-94 2015). The comonomer distribution can be determined by the ratio of the IR detector intensity corresponding to the CH3 and CH2 channels calibrated with a series of PE homo/copolymer standards whose nominal value was predetermined by NMR.

The detector produced separate and continuous streams of absorbance data, measured through each of their IR selective filters CH3 and CH2 at a fixed acquisition rate of one point per half second. The detector was equipped with a heated flow-through cell of 13 pL internal volume.

The ratio of infra-red absorbance band ratio A CH3 to A CH2 (methyl over methylene sensitive channels) can be correlated to the methyl (CH3) per 1000 total carbons (1000TC), denoted as CH3/IOOOTC, as a function of molecular weight.

The IR CH3/CH2 ratio of the polymer was obtained by considering the entire signals of the CH3 and CH2 channels between the integration limits of the concentration chromatogram:

IR ratio= Area of CH3 signal within integration limits/area of CH2 signal within integration limits. In the present invention, an increase of the area ratio CH3/CH2 means an increase in Short Chain Branching content.

Determination of Al and Zr contents

The Al and Zr contents were determined using inductively coupled plasma atomic emission spectroscopy (ICP-AES) after mineralization of the sample and recovery of the residues in an acid medium. The spectrometer used was ICP-AES ARCOS, by Spectro.

The determination of the elements was carried out by nebulization of the solution in an argon plasma, measurement of the intensities of the most sensitive and interference-free emission lines and comparison of these intensities with those of calibration solutions (external calibration method). of the test solution to be Under an inert atmosphere (in a glove box), about 0.3 g of catalyst were added into a platinum crucible and 3 to 5 mL of isopropyl alcohol were added to "deactivate" the catalyst. The mixture was heated to dryness in a sand bath (30 min). The platinum crucible was placed in an oven at 600°C for 10 min. After cooling, Milli-Q® deionized water was added to impregnate all the ashes, and 1 mL of concentrated HCI (Merck HCI 32% v/v) and concentrated HF (Merck HF 48% v/v) were added. The crucible was placed in a sand bath, and Milli-Q® deionized water was added to mix the content of the crucible. After 24 h, 1 mL of concentrated HCI, 0.5 mL of concentrated HF and

Milli-Q® deionized water were added while agitating the mixture under heat to achieve full dissolution. After cooling the mixture was transferred to a 50 mL polypropylene tube and the volume made up to 50 mL with Milli-Q® deionized water. The test solutions were then diluted 25 times ensuring that 2% HCI/HF1 % medium was maintained. Preparation of calibration standards and control solutions: Standard solutions were prepared by dilution of commercial single-element solutions of certified concentrations. The standard solutions were prepared by transferring the required volume of the certified solution to a 50 mL polypropylene tube, then rinsing the sides of the tube with Milli-Q® deionized water, and adding 1 mL of HCI and 0.5 mL of concentrated HF per 50 mL to obtain the same acid content in solution as in the sample solutions, and finalizing the dilution with Milli-Q® deionized water. Control solutions were prepared by dilution of commercial multi-element solutions of certified concentrations. The presence of other elements in solution allowed verification of the presence/absence of possible interferences. of results:

The content (in ppm) of the element measured in the sample was calculated as follows:

IT12

Concentration in— of the element in solution x Volume (50 mL)x Dilution factor

Mass (g)

The Limit of Quantification (LOQ) was calculated for each element from 10 blank measurements:

LOQ in solution (mg/l) = standard deviation of 10 replicates of the blank x 10

LQ in solution x Volume (50 mL)x Dilution factor

LOQ in sample (ppm) = - — - Mass (g)

CATALYSTS

Metallocene 1 (Butenyl)MeC(Cp)(2,7-tBu ₂ -Flu)ZrCI ₂ (Met1)

Metallocene 1 was prepared as described below, following the synthesis described in Journal of Organometallic Chemistry vol. 553, 1998, p. 205-220: Into a 200 mL 3-neck flask equipped with a gas inlet tube and a magnetic stirring bar was charged, under nitrogen, 2.5 eq of freshly cracked cyclopentadiene and 1 eq of 5-hexene-2- one in 60 mL of methanol. Then, 2 eq of pyrrolidine was added dropwise at 0 °C and the mixture was stirred overnight at room temperature. The reaction was quenched with 50 mL of HCI 1 M and extracted with Et20 (3 x 50 mL). Organic fractions were dried over MgSO4 and solvent was removed under reduced pressure. The fulvene was obtained as a yellow oil and used without further purification (Yield = 65%).

Step 2:

In a 3-neck flask, 1 eq of di-tert-butylfluorene was added under flow of nitrogen and dissolved in 70 mL of Et20. 1.1 eq of n-BuLi (1.6 M in hexane) was added dropwise at 0 °C to this solution and the mixture was stirred overnight at room temperature. A solution of 3.5 g of fulvene prepared in the previous step, dissolved in 30 mL of Et20 was added dropwise. The reaction mixture was allowed to stir overnight. Reaction was quenched with water and extracted with Et20 (3 x 50 mL). Combined organic fractions were dried over MgSCL and solvent was removed under reduced pressure. The product was crystallized in pentane/MeOH at 0 °C to afford a white solid (Yield = 85%).

Step 3:

In a round-bottomed flask, 1 g of ligand was introduced and dissolved in 40 mL of Et20. 2.1 eq. of nBuLi was added dropwise and the mixture was stirred overnight at room temperature. Solvent was removed under vacuum and 40 mL of dry pentane was added. Then 1 eq of ZrCL was added in small portions at room temperature. The reaction was stirred over 2 days and filtered. The resulting precipitate was diluted in DCM and centrifuged to eliminate lithium chloride. Solvent was removed under vacuum to afford a pink-red powder (Yield = 70%). ¹ H N MR (500 MHz, CD ₂ CI ₂ ) 6 1.34 (s, 9 H, CH ₃ tBu); 1.36 (s, 9 H, CH ₃ tBu); 2.30 (m, CH ₂ alk);

2.43 (s, 3 H, CH ₃ ); 2.55 (m, 1 H, CH ₂ alk.); 2.65 (m, 1 H, CH ₂ alk.); 3.25 (m, 1 H, CH ₂ alk.);

5.13 (m; 1 H, CHvinyl); 5.18 (m; 1 H, CHvinyl); 5.70 (m, 2 H, CHcp); 6.10 (m; 1 H, CHvinyl);

6.29 (m, 2 H, CHcp); 7.55 (s, 1 H, CHflu), 7.63-7.68 (m, 2 H, CHflu); 7.72 (s, 1 H, CHflu); 8.00- 8.04 (m, 2 H, CHflu)

Metallocene 2: rac-Cyclohexyl(methyl)silanediylbis[2-methyl-4-(4'-tert-buty lphenyl)indenyl]zirconium dichloride (Met2) was purchased from SPCI (South Pacific Chemical Industries) (CAS 888227- 55-2).

Metallocene 3: rac-dimethylsilanediyl-bis[(2-methyl-4-phenyl)-indenyl] ₂ zirconium dichloride (Met3) was purchased from Grace. (CAS 153882-67-8). Synthesis of supported catalysts

All catalyst and co-catalyst experimentations were carried out in a glove box under nitrogen atmosphere. Methylaluminoxane (30 wt.%) (MAO) in toluene from Albemarle was used as the activator. Titanated silica from PQ (PD12052) was used as catalyst support (D50: 25 pm). Supported metallocene catalysts were prepared in two steps using the following method:

1. Impregnation of MAO on silica:

Ten grams of dry silica (dried at 450 °C under nitrogen during 6 h) was introduced into a three necked a round-bottomed flask equipped with a mechanical stirrer and a slurry was formed by adding 100 mL of toluene. MAO (21 mL) was added dropwise with a dropping funnel. The reaction mixture was stirred at 110 °C for 4 h. The reaction mixture was filtered through a glass frit (POR3) and the powder was washed with dry toluene (3 x 20 mL) and with dry pentane (3 x 20 mL). The powder was dried under reduced pressure overnight to obtain a free-flowing grey powder.

2. Deposition of metallocene on silica/MAO support:

Silica/MAO (10 g) was suspended in toluene (100 mL) under nitrogen. Metallocene components A and B (total A+B= 200 mg) were introduced and the mixture was stirred 2 h at room temperature. The reaction mixture was filtered through a glass frit and the powder was washed with dry toluene (3 x 20 mL) and with dry pentane (3 times). The powder was dried under reduced pressure overnight to obtain a free-flowing grey powder.

The samples were analyzed for zirconium and aluminum content (wt.%) using ICP-AES spectroscopy (Inductively Coupled Plasma - Atomic Emission Spectroscopy). The results are shown in Table 1.

Table 1

POLYMERIZATIONS 1

Polymerization reactions were performed in a 132 mL autoclave with an agitator, a temperature controller, and inlets for feeding of ethylene and hydrogen. The reactor was dried at 110 °C with nitrogen for 1 h and then cooled to 40 °C.

All polymerizations were performed under the heterogenous conditions depicted in Table 2 (unless otherwise stated). The reactor was loaded with 75 mL of isobutane, 1.6 mL of 1-hexene (C6-) and pressurized with 23.8 bar of ethylene (C2-) with 800 ppm of hydrogen. Catalyst (3.5 mg) was added. Polymerization started upon catalyst composition suspension injection, and was performed at 85 °C. Polymerization was stopped after 60 min by reactor depressurization. Reactor was flushed with nitrogen prior opening. Table 2

*ln comparison to iC4 **in ethylene feed

The results of the co-polymerization of ethylene with 1 -hexene as comonomer in the presence of Met1/Met2 compositions with varying weight ratio of each catalyst are shown in Table 3.

Table 3

ND: not determined Figure 2 shows the GPC trace of the polymers obtained with dual catalyst composition Met1/Met2 having different catalyst weight ratio (from 50/50 to 20/80 Met1/Met2 weight ratio).

Figure 3 shows the GPC trace of the polymer obtained with dual catalyst composition with a 50/50 Met1/Met2 weight ratio. GPC-IR was used to determine the ratio of CH3 to CH2 groups at a given chain length, providing information on comonomer incorporation as a function of molecular weight. The tested polymer had an inverse comonomer incorporation.

The hydrogen response was studied. The results of the co-polymerization of ethylene with 1- hexene as comonomer in the presence of catalyst compositions Met1/Met2 as a function of hydrogen concentration are shown in Table 4 and Figure 4 (GPC trace) for the composition with a 50/50 Met1/Met2 weight ratio and in Table 5 and Figure 5 (GPC trace) for a composition with a 30/70 Met1/Met2 weight ratio. The polymerization conditions were the same as listed in

Table 2, except for the hydrogen concentration.

Table 4

ND: not determined Table 5

ND: not determined

The results of the homopolymerization of ethylene (using catalyst composition with a 50/50 Met1/Met2 weight ratio) as a function of hydrogen concentration are shown in Table 6, and Figure 6 (GPC trace). The polymerization conditions were the same as listed in Table 2, except that 0.0 % by weight of 1 -hexene was used.

Table 6

ND: not determined

POLYMERIZATIONS 2

Further polymerization reactions were performed using catalyst composition Met1/Met3 (50/50 weight ratio) (4.7 mg), using the conditions of Table 2. Results are detailed in Table 7, and GPC results are plotted in Figure 7.

Table 7