WO2014139949A1

WO2014139949A1 - Bis(2-indenyl) metallocene complex

Info

Publication number: WO2014139949A1
Application number: PCT/EP2014/054578
Authority: WO
Inventors: Haif Al-Shammari; Jason Morton; Douglas Stephan
Original assignee: Saudi Basic Industries Corporation; Sabic Petrochemicals B.V.
Priority date: 2013-03-12
Filing date: 2014-03-10
Publication date: 2014-09-18
Also published as: EP2970348A1; CN105073764A; JP2016516019A; RU2015143202A; US20140275455A1; BR112015019437A2; US9156929B2

Abstract

The invention relates to a metallocene complex according to the following formula (1), wherein R₁ and R₂ are the same or different and are independently selected from the group consisting of substituted and unsubstituted linear and branched hydrocarbyl groups comprising 1 to 30 carbon atoms; M is titanium, zirconium, or hafnium and X₁ and X₂ are the same and are selected from the group consisting of halogen and hydrocarbyl groups comprising 1 to 20 carbon atoms.

Description

BIS(2-INDENYU METALLOCENE COMPLEX

The invention relates to a metallocene complex, a process to prepare a metallocene complex, a process to produce olefin polymers by polymerizing one or more olefins in the presence of a metallocene complex and to polyethylene, preferably LLDPE obtainable by copolymerizing ethylene and at least one other olefin, preferably 1 -hexene in the presence of a metallocene complex.

Heterogeneous Ziegler-Natta titanium and Phillips chromium catalyst systems are currently utilized for the bulk of industrial linear polyethylene production. Great attention continues to be directed towards the synthesis and evaluation of homogeneous transition- metal catalysts. Such soluble, single-site metallocene catalysts are variable in their ligand scaffolding, allowing for the designed perturbation of the metal's electronic and structural environment. Soluble catalysts are of particular interest to complement the existing heterogeneous high- and low-density polyethylene (HDPE and LDPE) processes through the production of linear low-density polyethylene (LLDPE), where longer a-olefins such as 1 -butene, 1-hexene, and 1-octene are incorporated into the polyethylene chain. LLDPE has a density lower than about 0.94 g/cm³. Group 4 ansa-metallocenes with a single atom bridge are particularly well-studied. An ansa-metallocene is an organometallic compound containing two cyclopentadienyl- containing ligands that are linked by a bridging group such that both cyclopentadienyl groups are bound to the same metal. The link prevents rotation of the cyclopentadienyl ligands and often modifies the structure and reactivity of the metal center. Examples of such ansa metallocene catalysts are described in EP0653445A, EP0786466A,

W096/35729 and WO00/01736. In the last patent publication metallocene complexes of the general formula R"(CpR_m)(Cp'R'n)MQ₂ are described, wherein Cp is a cyclopentadienyl moiety, Cp' is a substituted or unsubstituted fluorenyl ring, R" is a structural bridge imparting stereorigidity to the component, each R is independently a hydrocarbyl having 1 to 20 carbon atoms in which 0<m<4, each R' is independently hydrocarbyl having 1 to 20 carbon atoms in which 0<n<8, M is a group IVB transition metal or vanadium and each Q is hydrocarbyl having 1 to 20 carbon atoms or halogen; the metallocene having a centroid- M-centroid angle in the range 105° to 125°. In the metallocene complexes according to WO00/01736 the bridge between the two Cp moieties is an alkylidene bridge having 1 to 20 carbon atoms, a dialkyl germanium or dialkyl silicone or siloxane bridge, an alkyl phosphine or alkyl amine.

The metallocene complexes according to the invention are metallocene complexes according to the following formula (1 )

wherein R-i and R₂ are the same or different and are independently selected from the group consisting of substituted and unsubstituted linear and branched hydrocarbyl groups comprising 1 to 30 carbon atoms;

M is titanium, zirconium, or hafnium and

and X₂ are the same and are selected from the group consisting of halogen and hydrocarbyl groups comprising 1 to 20 carbon atoms.

The bridge in the metallocene complexes according to the invention comprises a single, unsaturated carbon atom. This single unsaturated carbon atom in the bridge of the metallocene complexes according to the invention surprisingly has the effect that LLDPE can be obtained with a high molecular weight and a high comonomer incorporation.

The metallocene complex according to the invention is a complex according to the following formula (1 )

In this complex Ri and R₂ are the same or different and are independently selected from the group consisting of substituted and unsubstituted linear and branched hydrocarbyl groups comprising 1 to 30 carbon atoms.

The hydrocarbyl groups may be aliphatic or aromatic. The hydrocarbyl groups may also be cyclic in which case the hydrocarbyl groups preferably comprise 3 to 30 carbon atoms. Preferably, Ri and R₂ are linear hydrocarbyl groups, for example alkyl groups or cyclic aromatic hydrocarbyl groups comprising 1 to 30 carbon atoms. In one embodiment of the invention R-i and R₂ are linear hydrocarbyl groups, for example alkyl groups comprising 1 to 10 carbon atoms. Examples of these linear alkyl groups are methyl, ethyl, propyl, for example n-propyl, butyl, for example n-butyl and hexyl, for example n-hexyl.

In another embodiment of the invention R-i and R₂ are cyclic aromatic hydrocarbyl groups comprising 1 -20 carbon atoms. Examples of these cyclic aromatic hydrocarbyl groups are substituted and unsubstituted aryl groups, for example phenyl groups, indenyl groups or fluorenyl groups. Ri and R₂ may also form a ring together with the carbon atom to which they are bound to form a 5 or 6-membered ring which may be substituted or unsubstituted, for example Ri and R₂ may form an indenyl or a fluorenyl group, preferably fluorenyl together with the carbon atom to which they are bound.

Preferably, Ri and R₂ are selected from alkyl groups having 1 to 30 carbon atoms, for example from alkyl groups having 1 to 10 carbon atoms, for example Ri and R₂ may be selected from the group of methyl, ethyl, n-propyl, n-butyl, n-pentyl, n-hexyl, phenyl, 1 - indenyl and 2-indenyl. More preferably, Ri and R₂ are the same. Most preferably, Ri and R₂ are chosen from the group of n-propyl, n-butyl, n-pentyl and n-hexyl.

In the metallocene complex according to the invention M is chosen from titanium (Ti), zirconium (Zr), or hafnium (Hf). Preferably, M is titanium.

In the metallocene complex X-_\ and X₂ are preferably the same and are selected from the group consisting of halogen and hydrocarbyl groups comprising 1 to 20 carbon atoms, for example from the group consisting of linear alkyl groups comprising 1 to 20 carbon atoms and a cyclic aromatic group comprising 3 to 20 carbon atoms, for example an aryl group, for example phenyl. Preferably, Xi and X₂ are each independently selected from the group of methyl and halogen, preferably CI or Br, more preferably CI. More preferably, Xi and X₂ are the same and both stand for methyl or for a halogen, even more preferably Xi and X₂ both stand for CI or for Br, even more preferably Xi and X₂ both stand for CI.

The metallocene complex can be supported on a support. The support is preferably an inert support, more preferably a porous inert support. Examples of porous inert supports materials are talc and inorganic oxides. Preferably, the support material is in a finally divided form.

Therefore, the invention also relates to a composition comprising the metallocene complex of the invention, wherein the metallocene complex is present on a support.

Suitable inorganic oxide materials include group 2A, 3A, 4A and 4B metal oxides such as silica, alumina and mixtures thereof. Other inorganic oxides that may be employed either alone or in combination with the silica or alumina are magnesia, titania, zirconia and the like. Other support materials, however, can be employed, for example finely divided functionalized polyolefins such as finely divided polyethylene.

Preferably, the support is a silica having a surface area between 200 and 900 m²/g and a pore volume between 0.5 and 4 ml/g.

The invention further relates to a process for the preparation of a metallocene complex according to the invention, comprising the steps of

a. transforming 2-bromoindene to the corresponding Grignard reagent 2-indeneMgBr b. reacting 2-indeneMgBr with tri-n-butylchloride to give (2-C₉H₇)Mg(n-butyl)₃ c. reacting (2-C₉H₇)Mg(n-butyl)₃ with R₂ under Pd catalyzed conditions to form ligand precursors,

d. creating anions of the ligand precursors with natriumhexametyldisiloxane

e. reacting the anion of the ligand precursor with (Me₂N)₂MCl₂ , wherein M stands for titanium (Ti), zirconium (Zr) or hafnium (Hf) and thereafter with trimethylsilylchloride to yield a metallocene complex according to any one of claims 1-6.

The process steps are also given in the enclosed Scheme 1 . In another aspect, the invention relates to a process for the preparation of olefin polymers by polymerizing one or more olefins in the presence of the metallocene complex of the invention or in the presence of the composition of the invention, wherein the metallocene complex is present on a support and a cocatalyst The cocatalyst employed according to the present invention include aluminium- or boron- containing cocatalysts. Suitable aluminium-containing cocatalysts comprise aluminoxanes and alkyl aluminium. The aluminoxanes usable according to the present invention are well known an preferably comprise oligomeric linear and/or cyclic alkyl aluminoxanes represented by the formula: R³ - (AIR³ -0)_n - AIR³ ₂for oligomeric, linear aluminoxanes and

(- AIR³ - O -)_mfor oligomeric, cyclic aluminoxanes; wherein n is 1-40, preferably n is 10-20; m is 3-40, preferably m is 3-20 and R³ is a C-i to C₈ alkyl group and preferably a methyl group. Further other organoaluminum compounds can be used such as

trimethylaluminum, triethylaluminium, triisopropylaluminum, tri-n-propylaluminum, triisobutylaluminum, tri-n-butylaluminum, triamylaluminium; dimethylaluminium ethoxide, diethylaluminium ethoxide, diisopropylaluminium ethoxide, di-n-propylaluminium ethoxide, diisobutylaluminium ethoxide and di-n-butylaluminium ethoxide;

dimethylaluminium hydride, diethylaluminium hydride, diisopropylaluminium hydride, di-n- propylaluminium hydride, diisobutylaluminium hydride and di-n-butylaluminium hydride.

Suitable boron-containing cocatalysts are trialkylboranes, for example trimethylborane or triethylborane.

In the process to produce olefin polymers by polymerizing one or more olefins in the presence of a metallocene complex preferably an organoaluminum cocatalyst is present.

More preferably, methylaluminoxane is used as the cocatalyst. The process to produce the olefin polymers preferably starts with the reaction of the metallocene complex according to the invention with the cocatalyst. This reaction can be performed in the same vessel as the reaction vessel wherein the olefin polymers are produced or in a separate vessel, whereafter the mixture of the metallocene complex and the cocatalyst is fed to the reaction vessel. During the reaction described above an inert solvent can be used.

In the mixture of the metallocene complex and the cocatalyst, the cocatalyst is used in an amount of 10 to 100,000 mol, preferably from 10 to 10,000 mol per mol of the transition metal compound.

The solvent used in the process to produce olefin polymers may be any organic solvent usually used for the polymerization. Examples of solvents are benzene, toluene, xylene, butane, pentane, hexane, heptane, cyclohexane and methylene chloride. Also the olefin to be polymerized can be used as the solvent.

In the process to produce olefin polymers the polymerization conditions, like for example temperature, time, pressure, monomer concentration can be chosen within wide limits. The polymerization temperature is in the range from -100 to 300 °C, preferably 0 to 200 °C, more preferably 10 to 100 °C. The polymerization time is in the range of from 10 seconds to 20 hours, preferably from 1 minute to 10 hours, more preferably from 5 minutes to 5 hours. The ethylene pressure during polymerization is in the range from 1 to 3500 bar, preferably from 1 to 2500 bar, more preferably from 1 to 1000 bar, even more preferably from 1 to 500 bar, most preferably from 1 to 100 bar. The molecular weight of the polymer can be controlled by use of hydrogen in the polymerization. The polymerization may be conducted by a batch process, a semicontinuous process or a continuous process and may also be conducted in two or more steps of different polymerization conditions. The polyolefin produced is separated from the polymerization solvent and dried by methods known to a person skilled in the art. In the process to produce olefin polymers the olefin which is polymerized can be one type of olefin or can be mixtures of different olefins. The polymerization thus includes homopolymerization and copolymerization. Examples of olefins are oolefins such as ethylene, propylene, 1-butene, 1 -pentene, 4-methyl-1 -pentene, 1-hexene, 1-octene, 1 - nonene, 1-decene and styrene; conjugated and non-conjugated dienes such as butadiene, 1 ,4-hexadiene, 5-ethylidene-2-norbornene, dicyclopentadiene, 4-methyl-1 ,4-hexadiene and 7-methyl-1 ,6-octadiene; and cyclic olefins such as cyclobutene, but is not limited thereto. Preferably, at least one of the olefins that is polymerized is ethylene. More preferably, a mixture of ethylene and at least one other olefin is polymerized. The other olefin is preferably chosen from 1-butene, 1 -hexene or 1 -octene, more preferably the other olefin is 1-hexene. In particular, in the production of LLDPE obtained by copolymerizing ethylene and an olefin of 3 or more carbon atoms a high molecular weight of the olefin polymer can be obtained. Preferably, the olefin of 3 or more carbon atoms is chosen from 1-butene, 1- hexene or 1-octene, more preferably the other olefin is 1 -hexene. Preferably, the olefin comonomer is present in an amount of about 5 to about 20 percent by weight of the ethylene-olefin copolymer, more preferably an amount of from about 7 to about 15 percent by weight of the ethylene-alpha olefin copolymer.

For example an LLDPE having a melt mass flow rate (also known as melt flow index) as determined using ASTM D1238-10 (190°C/2.16 kg) which ranges from 4 to 125 g/10 min and a density in the range from 900 kg/m³ to less than 940 kg/m³ as determined using ASTM D1505-10 may be obtained. For example, the density of the linear low density polyethylene ranges from about 915 kg/m³ to less than 940 kg/m³. Preferably, the melt flow index of the linear low density polyethylene ranges from 0.3 to 3 g/10min, for example from 0.5 to 1.5 g/10min. For purpose of the invention, the melt flow index is determined herein using IS01 133:201 1 (190°C/2.16kg).

The polymerisation may be performed via a gas phase process or via a slurry process. Gas fluidized bed polymerisation processes are summarised by Than Chee Mun in Hydrocarbons 2003 "Production of polyethylene using gas fluidised bed reactor". Gas phase polymerisation generally involves adding gaseous monomers into a vertically oriented polymerisation reactor filled with previously formed polymer, catalyst particles and additives. Generally the polymerisation in the gas phase polymerisation systems takes place at temperatures between 30 °C and 130 °C with super atmospheric pressures. The rising gas phase fluidizes the bed, and the monomers contained in the gas phase polymerize onto supported catalyst or preformed polymer during this process. Upon reaching the top of the reactor, unreacted monomer is recycled, while polymer continually falls down along the sides of the reactor. Examples of suitable gas phase polymerisations are disclosed in for example US-A- 4003712 and US-A- 2005/0137364.

In slurry reactors, a low boiling hydrocarbon solvent such as isobutane, hexane or heptane is employed as a continuous medium, and monomer, catalyst etc. is added to this continuous phase. The polymer formed is insoluble in the reaction medium, producing slurry of polymer and catalyst. Slurry reactors may be divided into loop reactors and boiling solvent reactors. Heat is at least partially removed by the heat of vaporization of solvent, which is later condensed and returned to the reactor. Polymer is removed as slurry from the bottom of the reactor and flashed to remove solvent, which is recycled. Slurry loop reactors may be horizontally or vertically oriented. Water flowing between the tubes serves to remove heat and maintain a relatively constant temperature. Slurry flow is achieved by pumps which maintain the polymer slurry at relatively high velocity. Product is removed either continuously or discontinuously from a "settling leg." Preferably, the polymerization with the metallocene complex according to the invention is a polymerization via a slurry process.

Hydrogen gas may also be added to the polymerization reactor(s) to control the final properties (e.g., 121 and/or I2) of the polyethylene composition. In one embodiment, the ratio of hydrogen to total ethylene monomer (ppm H₂ / mol % C₂) in the circulating gas stream is in a range of from 0 to 60:1 in one embodiment; from 0.10:1 (0.10) to 50:1 (50) in another embodiment; from 0 to 35:1 (35) in another embodiment; from 0 to 25:1 (25) in another embodiment; from 7:1 (7) to 22:1 (22). The invention is also directed to a polyolefin, for example polyethylene, preferably LLDPE or LDPE obtainable or obtained by the process of the invention, for example by copolymerizing ethylene and at least one other olefin in the presence of a metallocene complex according to the invention or a composition, wherein the metallocene complex is present on a support according to the invention.

As defined herein, in linear low density polyethylene, the term "linear" means that the polymer lacks measurable or demonstrable long chain branches, that is, the polymer is substituted with an average of less than 0.01 long chain branch/1000 carbon atoms.

"Long chain branching" (LCB) means a chain length longer than the short chain branch that results from the incorporation of the oolefin(s) into the polymer backbone. Each long chain branch will have the same comonomer distribution as the polymer backbones and can be as long as the polymer backbone to which it is attached.

As a practical matter, current ¹³C nuclear magnetic resonance spectroscopy cannot distinguish the length of a long chain branch in excess of six carbon atoms. However, there are other known techniques useful for determining the presence of long chain branches in ethylene polymers. Two such methods are gel permeation chromatography coupled with a low angle laser light scattering detector (GPC-LALLS) and gel permeation chromatography coupled with a differential viscometer detector (GPCDV). The use of these techniques for long chain branch detection and the underlying theories have been well documented in the literature. See, for example, Zimm, G.H. and Stockmayer, W.H., J.Chem. Phys., 17, 1301 (1949) and Rudin, A., Modern Methods of Polymer Characterization, John Wiley & Sons, New York (1991 pp. 103-1 12).

It has been found that with the metallocene complex of the invention or with the composition of the invention wherein the metallocene complex of the invention on a support, it is possible to produce polyethylene from ethylene and at least one other olefin, for example an olefin having up to 8 carbon atoms, with a high incorporation of the at least one other olefin. The amount of incorporation of the at least one other olefin, for example an oolefin in the polyethylene is expressed by the amount of branches per 1000 carbon atoms.

It has been found that in the polyethylene, for example LDPE or LLDPE of the invention, the amount of branches per 1000 carbon atoms is high.

The presence of short chain branching of up to 6 carbon atoms in length can be determined in ethylene polymers by using ¹³C nuclear magnetic resonance (NMR) spectroscopy and is quantified using the method described by Randall (Rev. Macromol. Chem. Phys., C.29, V. 2 & 3, p. 285-297).

Therefore, the invention also relates to a polyolefin, for example polyethylene, for example LDPE or LLDPE, having an amount of branches per 1000 carbon atoms as determined using ¹³C NMR of at least 18, for example of at least 18, for example at least 19, for example at least 20 and/or for example at most 30, for example at most 25, for example at most 23, for example at most 21. Preferably, said polyethylene is substituted with an average of less than 0.01 long chain branch per 1000 carbon atoms.

The number average molecular weight (Mn) of the polyolefin, for example polyethylene, for example LDPE or LLDPE of the invention may vary between wide ranges and may for example be in the range from 1000 to 200000Da.

For example, the Mn of the polyolefin of the invention may be at least 1500, for example at least 2000, for example at least 20,000, for example at least 50,000 and/or for example at most 150,000, for example at most 1 10,000, for example at most 100,000, for example at most 70,000.

The weight average molecular weight (Mw) of the polyolefin, for example polyethylene, for example LDPE or LLDPE of the invention may also vary between wide ranges and may for example be in the range from 1500 to 500000. For example, the Mw of the polyolefin of the invention may be at least 2500, for example at least 10,000, for example at least

50,000, for example at least 100,000 and/or for example at most 400,000, for example at least 350,000, for example at most 300,000, for example at most 250,000.

For purpose of the invention, the Mw and Mn are determined using SEC (Size Exclusion Chromatrography using 1 ,2,4-trichlorobenzene as an eluent, and calibrated using linear polyethylene standards.

The molecular weight distribution (that is Mw/Mn) of the polyolefin of the invention may for example vary from 1 .5 to 3.5, for example the molecular weight distribution (MWD) may range from 1.5 to 2.0 or from 2 to 3.5 or from 2.5 to 3.5.

The crystallinity temperature (Tc) of the polyolefin of the invention may for example be in the range from 90 to 120°C. The melt temperature (Tm) of the polyolefin of the invention may for example be in the range from 100 to 140°C.

For purpose of the invention, the T_m and T_c are determined using Differential Scanning Calorimetry according to ASTM D 3418-08 using a scan rate of 10°C/min on a sample of 10mg and using the second heating cycle

The degree of crystallinity of the polyolefin of the invention may for example be in the range of 10 to 90%, for example at least 40% and/or for example at most 65%.

For purpose of the invention, the degree of crystallinity is determined using Differential Scanning Calorimetry according to ASTM D 3418-08 using a scan rate of 10°C/min on a sample of 10mg and using the second heating cycle.

The polyolefin obtained or obtainable by the process of the invention may be mixed with suitable additives.

Examples of suitable additives for polyethylene include but are not limited to the additives usually used for polyethylene, for example antioxidants, nucleating agents, acid scavengers, processing aids, lubricants, surfactants, blowing agents, ultraviolet light absorbers, quenchers, antistatic agents, slip agents, anti-blocking agents, antifogging agents, pigments, dyes and fillers, and cure agents such as peroxides. The additives may be present in the typically effective amounts well known in the art, such as 0.001 weight % to 10 weight % based on the total composition.

The polyolefins of the invention and compositions comprising said polyolefins may suitably be used for the manufacture of articles. For example, the polyolefins and compositions of the invention may be manufactured into film, for example by compounding, extrusion, film blowing or casting or other methods of film formation to achieve, for example uniaxial or biaxial orientation. Examples of films include blown or cast films formed by coextrusion (to form multilayer films) or by lamination and may be useful as films for packaging, for example as shrink film, cling film, stretch film, sealing films, oriented films, snack packaging, heavy duty bags, grocery sacks, baked and frozen food packaging, medical packaging, industrial liners, membranes, etc. in food-contact and non-food contact applications, agricultural films and sheets.

Therefore, in another aspect, the invention also relates to articles comprising the polyolefins obtainable by the process of the invention.

In yet another aspect, the invention also relates to use of the polyolefins obtainable by the process of the invention for the preparation of articles, for example for the preparation of films.

In yet another aspect, the invention relates to a process for the preparation of articles using the polyolefin according to the invention.

Although the invention has been described in detail for purposes of illustration, it is understood that such detail is solely for that purpose and variations can be made therein by those skilled in the art without departing from the spirit and scope of the invention as defined in the claims.

It is further noted that the invention relates to all possible combinations of features described herein, preferred in particular are those combinations of features that are present in the claims. It is further noted that the term 'comprising' does not exclude the presence of other elements. However, it is also to be understood that a description on a product comprising certain components also discloses a product consisting of these components. Similarly, it is also to be understood that a description on a process comprising certain steps also discloses a process consisting of these steps. The invention will hereafter be elucidated by way of the following examples, without being limited thereto. Examples

Example I

Ligand Synthesis

This synthesis is also elucidated in Scheme 1. To synthesize the ligands, 2-bromoindene (1) was first transformed to the corresponding Grignard reagent, then transmetallated with tri-n-butyltin chloride to give the stannane (2- C₉H₇)SnBu₃ (2). Migita-Kosugi-Stille cross-couplings with the gem-dibromides 3-5, were then accomplished under palladium-catalyzed conditions, providing the ligand precursors R₂C=C(2-C₉H₇)2 (R = Ci₂H₈ 6, Ph 7, n-Pr 8). It is noteworthy that attempts to use 1 H- inden-2-ylboronic acid or its trifluoroborate salt for this later transformation gave very low yields.

The ligand dianions were most effectively generated by deprotonation with sodium hexamethyldisilazine (NaHMDS). Though subsequent salt metathesis with the simple TiCI₃, TiCI₄, or ZrCI₄ gave inconsistent results, reactions with (Me₂N)₂TiCl₂ and

(Me₂N)₂ZrCI₂ ^«DME yielded the desired ansa-metallocenes. Finally, treatment with trimethylsilyl chloride provided the dichlorides R₂C=C(2-C₉H₇)₂MCI₂ (R = C₁₂H₈, M = Ti: 9a, Zr: 9b; R = Ph, M = Ti: 10a, Zr: 10b; R = n-Pr, M = Ti: 11a, Zr: 11 b) in yields ranging from 36-89%.

All complexes were characterized by ¹H- and ¹³C-NMR spectroscopy and elemental analysis.

Compounds 2-bromoindene (1 ), 9-(dibromomethylene)fluorene (3), (2,2-dibromoethene- 1 , 1-diyl)dibenzene (4), 4-(dibromomethylene)heptane (5), (Me₂N)₂ZrCI₂ ^«2DME, and (Me₂N)₂TiCI₂were prepared according to literature (See Mc Ewen, I.; Roennqvist, M.; Ahlberg, P. J Am Chem Soc 1993, 115, 3989; Paul, G. C; Gajewski, J. J. Synthesis 1997, 524; Donovan, P. M.; Scott, L. T. J. Am. Chem. Soc. 2004, 126, 3108; Rezaei, H.;

Normant, J. F. Synthesis 2000, 109. Warren, T. H.; Erker, G.; Frohlich, R.; Wibbeling, B. Organometallics 2000, 19, 127; Benzing, E.; W., K. Chem. Ber. 1961 , 94, 2263; Wang, C; Erker, G.; Kehr, G.; Wedeking, K.; Frohlich, R. Organometallics 2005, 24, 4760). All reactions were carried out and all metallocene complexes were manipulated under an atmosphere of anhydrous N₂ unless otherwise noted. Hexanes, /so-pentane, THF, Et₂0, PhMe, and CH₂CI₂ were dried and deoxygenated using a solvent purification system in the manner of Grubbs (Pangborn, A. B.; Giardello, M. A.; Grubbs, R. H.; Rosen, R. K.;

Timmers, F. J. Organometallics 1996, 15, 1518), while PhH, PhCI, and 1 -hexene were distilled from CaH₂. All solvents were degassed and held over 4 A molecular sieves prior to use. All other reagents were commercially obtained and used as received. Preparative flash chromatography was performed on Silicycle P60 40— 63 μηη silica gel. NMR analysis was obtained on Varian Mercury 400, Unity 500, and Bruker Avance III 400 spectrometers. Elemental analysis was performed by the University of Toronto, ANALEST facility, using a PerkinElmer 2400 Series II CHNS Analyzer. Example II

Synthesis of (C₉H₇)SnBu₃ (2)

A Schlenk flask was charged with a magnetic stir bar and Mg turnings (5.6 g, 231 mmol, 3.0 eq.) and flame-dried under vacuum. After cooling, the flask was purged to N₂, anhydrous THF was added to just cover the turnings, and stirring was commenced. Two drops of 1 ,2-dibromoethane were added as initiator, and a heat gun used to briefly reflux the contents, after which the flask was placed in a 25 °C water bath. In a separate flame- dried flask under N₂ atmosphere, 2-bromoindene (1 , 15.0 g, 76.9 mmol, 1 .0 eq.) was dissolved in 75 ml. anhydrous THF. A cannula was then used to transfer this solution onto the activated magnesium turnings over 45 min, resulting in a red, opaque solution. After 1.5 h, GC/MS analysis of an aliquot sample showed consumption of the 2-bromoindene. A separate flame-dried flask under N₂ atmosphere was charged with n-Bu₃SnCI (22.9 ml_, 84.6 mmol, 1 .1 eq.) in 75 ml. anhydrous THF and cooled to 0 °C. To this was added, by cannula, the Grignard solution over 20 min., and the reaction flask was brought to ambient temperature for an additional 20 min. The mixture was quenched with chilled, saturated aq. NH₄CI and the organics were separated with Et₂0/brine x3. The combined organic layers were dried with anhydrous MgS0₄, filtered, and concentrated to an orange oil. This was pushed through a plug of activated, neutral alumina using hexanes, to provide, after removal of volatiles, the stannane 2 as a yellow oil (27.7 g, -95 weight% purity by NMR) which was used without further purification. (The product is unstable to normal Si0₂ chromatography, while an attempt at vacuum distillation was unsuccessful). ¹H-NMR (300 MHz, CDCI₃) δ 7.51 (d, J = 7.3 Hz, 1 H), 7.42 (d, J = 7.4 Hz, 1 H), 7.29 (t, J = 7.3 Hz, 1 H), 7.17 (td, J = 7.4, 1.1 Hz, 1 H), 7.09 (s, 1 H), 3.52 (d, J = 1.8 Hz, 2H), 1 .79 - 1 .49 (m, 6H), 1 .47 - 1.29 (m, 6H), 1.1 1 - 1.12 (m, 6H), 0.94 (t, J = 7.3 Hz, 9H). ¹³C-NMR (75 MHz,

CDCI₃)5 149.92, 147.00, 145.56, 141.81 (J_C-sn = 16.4 Hz), 126.06, 123.92, 123.21 , 1 19.97, 45.85 (Jc-sn = 20.8, 20.0 Hz), 29.23 (J_C-sn = 10.5 Hz), 27.36 (J_C-sn = 28.5, 27.2 Hz), 13.69, 9.69 (Jc-sn = 173, 166Hz). Example III

Synthesis of

(6)

In a flame-dried Schlenk flask under N₂ atmosphere were combined 9- (dibromomethylene)fluorene (3) (2.0 g, 5.95 mmol, 1.0 eq.) and tributyl(1 /- -inden-2- yl)stannane (2) (6.03 g, 14.9 mmol, 2.5 eq.). Magnetic stirring commenced, and the contents were degassed under vacuum for 15 min. The flask was purged with N₂, then charged with 30 mL anhydrous, degassed toluene. Tris(dibenzylideneacetone)dipalladium (Pd₂(dba)₃) (272 mg, 0.30 mmol, 0.05 eq.) and i-Bu₃P (240 mg, 1 .2 mmol, 0.2 eq.) were combined in 3 mL anhydrous, degassed toluene and syringed into the reaction mixture. This was followed by three freeze-pump-thaw cycles, then reintroduction of N₂

atmosphere. The reaction mixture was then heated at 100 °C for 14 h. After this time, the solution was allowed to cool to ambient temperature, and KF (3.46 g, 59.5 mmol, 10 eq.) and 30 mL H₂0 were added and the resultant biphasic mixture was stirred vigorously for 1 h. The crude product was then filtered through Celite, with ethylacetate (EtOAc) as additional elutant. After aqueous separation with brine, the organic layer was dried with MgS0₄ and concentrated by rotary evaporation onto 2 g of silica. Column chromatography (5 -> 10 -> 20 -> 30% PhMe/hexanes; the product can be seen as a red band) provided the desired 6 (2.05 g, 85% yield) as a bright red solid. ¹H-NMR (200 MHz, CDCI₃) δ 7.73 (d, J = 7.5 Hz, 2H), 7.46 (dd, J = 7.5, 5.2 Hz, 6H), 7.40 - 7.19 (m, 6H), 7.13 - 6.98 (m, 4H), 3.72 (s, 4H). ¹³C-NMR (101 MHz, CDCI₃) δ 148.45, 144.73, 143.99, 140.25, 138.49, 137.06, 134.96, 133.40, 127.67, 126.80, 125.35, 124.80, 123.96, 121.70, 1 19.49, 40.95. Analysis Calc'd for C₃₂H₂₂ (406.52 g/mol): C, 94.55; H, 5.45; Found: C, 94.08; H, 5.83.

Example IV

Synthesis of Ph₂C=C(C₉H₇)₂ (7) In a flame-dried Schlenk flask under N₂ atmosphere were combined (2,2-dibromoethene- 1 , 1-diyl)dibenzene (4) (1.0 g, 2.96 mmol, 1.0 eq.) and tributyl(1 /-/-inden-2-yl)stannane (2) (3.00 g, 7.40 mmol, 2.5 eq.). Magnetic stirring was commenced, and the contents were degassed under vacuum for 15 min. The flask was purged with N₂, then charged with 15 mL anhydrous, degassed toluene. Pd₂(dba)₃ (136 mg, 0.15 mmol, 0.05 eq.) and /-Bu₃P (120 mg, 0.59 mmol, 0.2 eq.) were combined in 1.5 mL anhydrous, degassed toluene and syringed into the reaction mixture. This was followed by three freeze-pump-thaw cycles, then reintroduction of N₂ atmosphere. The reaction mixture was then heated at 100 °C for 14 h. After this time the solution was allowed to cool to ambient temperature, then KF (1.72 g, 29.6 mmol, 10 eq.) and 15 mL H₂0 were added and the resultant biphasic mixture was stirred vigorously for 1 h. The crude product was then filtered through Celite, with EtOAc as additional elutant. After aqueous separation with brine, the organic layer was dried with MgS0₄ and concentrated by rotary evaporation onto 3 g of silica. Column chromatography (5 -> 10 -> 20 -> 30 -> 40% PhMe/hexanes; the product can be seen as a yellow band) provided the desired 7 (840 mg, 70% yield) as a bright yellow solid. ¹H-

NMR (400 MHz, CDCI₃) δ 7.43 - 7.27 (m, 16H), 7.24 (td, J = 7.2, 1 .5 Hz, 2H), 6.84 (s, 2H), 3.34 (s, 2H). ¹³C-NMR (101 MHz, CDCI₃) δ 150.00, 144.61 , 143.86, 143.77, 141.27, 134.1 1 , 133.06, 130.45, 128.06, 126.98, 126.23, 124.54, 123.36, 120.86, 41.25. Analysis Calc'd for C₃₂H₂₄ (408.53 g/mol): C, 94.08; H, 5.92; Found: C, 93.61 ; H, 6.21.

Example V

Synthesis of n-Pr₂C=C(C₉H₇)₂ (8)

In a flame-dried Schlenk flask under N₂ atmosphere were combined 4- (dibromomethylene)heptane (5) (1.0 g, 3.70 mmol, 1.0 eq.) and tributyl(1 /- -inden-2- yl)stannane (2) (3.75 g, 9.26 mmol, 2.5 eq.). Magnetic stirring commenced, and the contents were degassed under vacuum for 15 min. The flask was purged with N₂, then charged with 18.5 mL anhydrous, degassed toluene. Pd₂(dba)₃ (169 mg, 0.185 mmol, 0.05 eq.) and f-Bu₃P (150 mg, 0.74 mmol, 0.2 eq.) were combined in 1 mL anhydrous, degassed toluene and syringed into the reaction mixture. This was followed by three freeze-pump-thaw cycles, then reintroduction of N₂ atmosphere. The reaction mixture was then heated at 100 °C for 20 h. After this time, the solution was allowed to cool to ambient temperature, and KF (2.15 g, 37.0 mmol, 10 eq.) and 20 mL H₂0 were added and the resultant biphasic mixture was stirred vigorously for 1 h. The crude product was then filtered through Celite, with EtOAc as additional elutant. After aqueous separation with brine, the organic layer was dried with MgS0₄ and concentrated by rotary evaporation onto 2 g of silica. Column chromatography (5% PhMe/hexanes) provided the desired 8 (704 mg, 56% yield) as a slightly yellow, viscous oil. ¹H-NMR (400 MHz, CDCI₃) δ 7.30 (d, J = 7.4 Hz, 1 H), 7.23 (dd, J = 14.1 , 7.3 Hz, 2H), 7.1 1 (td, J = 7.4, 1 .1 Hz, 1 H), 6.64 (s, 1 H), 3.26 (s, 2H), 2.36 - 2.04 (m, 2H), 1 .56 - 1.36 (m, 2H), 0.84 (t, J = 7.3 Hz, 3H). ¹³C-NMR (100 MHz, CDCI₃) 5 148.78, 145.60, 143.65, 141 .13, 130.83, 129.89, 126.80, 124.66, 123.85, 121 .04, 42.51 , 34.94, 22.53, 14.31. Analysis Calc'd for C₂₆H₂₈ (340.50 g/mol): C, 91.71 ; H, 8.29; Found C, 91.30; H 8.40. Example VI

Synthesis of (Ci₂H8)C=C(C₉H₆)2TiCl2 (9a)

In the glovebox, under N₂ atmosphere, a vial was charged with 9-(di(1 /- -inden-2- yl)methylene)fluorene (6) (73 mg, 0.180 mmol, 1.0 eq.) and 3.6 ml. THF. The mixture was stirred magnetically and cooled to -35 °C, after which time solid NaHMDS (69 mg, 0.377 mmol, 2.1 eq.) was added in one portion. The reaction was allowed to warm slowly to ambient temperature and stirred for a total time of 5 h. The homogenous solution was then cooled back to -35 °C and solid (Me₂N)₂TiCI₂ (39.1 mg, 0.189 mmol, 1 .05 eq.) was added. The reaction mixture was allowed to warm slowly to ambient temperature and stirred overnight. After this time, the THF was removed in vacuo. The residue was filtered through Celite with PhH, concentrated, and washed with 2 ml. portions of pentanes (x5) to remove trace remaining (Me₂N)₂TiCI₂. The resultant dark purple residue was dissolved in 1.5 ml_ CH₂CI_2, after which Me₃SiCI (0.06 ml_, 0.46 mmol, 3.0 eq.) was added. The reaction mixture was stirred magnetically for 12 h, then the volatiles were removed in vacuo. The purple residue was added to a small pipet packed with Celite. It was washed with PhH, which was then discarded. The remaining solids were then filtered through using PhCI, which after concentration and precipitation from hexanes provided 9a (38 mg, 48% yield) as a purple solid. Crystals suitable for X-ray diffraction could be grown by vial-in-vial solvent diffusion of a concentrated solution of 9a in PhCI with hexanes. ¹H-NMR (500 MHz, C₆D₅Br) δ 7.84 (d, J = 7.7 Hz, 2H), 7.81 (d, J = 7.6 Hz, 2H), 7.73 (dd, J = 6.5, 3.1 Hz, 4H), 7.47 (dt, J = 7.6, 1.1 Hz), 7.30 (dd, J = 6.4, 3.1 Hz, 2H), 7.17 (dt, J = 7.6, 1 .1 Hz, 2H), 6.24 (s, 4H). ¹³C-NMR (partial, by gHMBC; C₆D₅Br) δ 141 .5, 137.4, 133.9, 130.0, 128.4, 127.9, 126.3, 125.3, 120.7, 1 13.1 , 109.4. Analysis Calc'd for C₃₂H₂₀CI₂Ti · C₆H₅CI (634.05 g/mol): C, 71.78; H, 3.96; Found: C, 71.92; H, 4.39. Example VII

Synthesis of Ph₂C=C(C₉H₆)2TiCl2 (10a)

In the glovebox, under N₂ atmosphere, a vial was charged with 2,2'-(2,2-diphenylethene- 1 , 1 -diyl)bis(1 H-indene) (7) (147 mg, 0.360 mmol, 1 .0 eq.) and 7.2 mL THF. The mixture was stirred magnetically and cooled to -35 °C, after which time solid NaHMDS (139 mg, 0.756 mmol, 2.1 eq.) was added in one portion. The reaction was allowed to warm slowly to ambient temperature and stirred for a total time of 4 h. The homogenous solution was then cooled back to -35 °C and solid (Me₂N)₂TiCI₂ (78 mg, 0.378 mmol, 1 .05 eq.) was added. The reaction mixture was allowed to warm slowly to ambient temperature and stirred overnight. After this time, the THF was removed in vacuo. The residue was washed over a plug of Celite with hexanes, and the elutant discarded. The remaining residue was then washed through with PhH. The solvent was removed and the yellow/brown solid taken up in 2.4 ml. CH₂CI_2, after which trimethylsilylchloride (0.091 ml_, 0.720 mmol, 3.0 eq.) was added. The reaction mixture was stirred magnetically for 12 h, then the volatiles were removed in vacuo. The dark residue was added to a small pipet packed with Celite. It washed with a 3:1 pentane/Et₂0 solution, which was then discarded. The remaining solids were then filtered through using CH₂CI₂, which after concentration provided 10a (68 mg, 36% yield) as a purple solid. Crystals suitable for X-ray diffraction could be grown by layering hexanes over a concentrated solution of 10a in CH₂CI₂. ¹H-NMR (400 MHz, CD₂CI₂) δ 7.58 - 7.53 (m, 4H), 7.49 (dd, J = 6.5, 3.1 Hz, 4H), 7.40 - 7.26 (m, 10H), 6.18 (s, 4H). ¹³C-NMR (101 MHz, CD₂CI₂)5 144.60, 139.39, 133.72, 130.41 , 128.92, 128.87, 128.78, 128.1 1 , 127.16, 126.07, 1 14.83, 1 10.89. Analysis Calc'd for C₃₂H₂₂CI₂Ti · CH₂CI₂ (612.24): C, 64.95; H, 3.96; Found: C, 64.43; H, 3.84. Example VIII

Synthesis of n-Pr₂C=C(C₉H₆)₂TiCI₂ (11 a)

In the glovebox, under N₂ atmosphere, a vial was charged with 2,2'-(2-propylpent-1 -ene- 1 , 1 -diyl)bis(1 H-indene) (8) (206 mg, 0.605 mmol, 1 .0 eq.) and 12 mL THF. The mixture was stirred magnetically and cooled to -35 °C, after which time solid NaHMDS (233 mg, 1.27 mmol, 2.1 eq.) was added in one portion. The reaction was allowed to warm slowly to ambient temperature and stirred for a total time of 6 h. The homogenous solution was then cooled back to -35°C and solid (Me₂N)₂TiCI₂ (131 mg, 0.635 mmol, 1.05 eq.) was added. The reaction mixture was allowed to warm slowly to ambient temperature and stirred overnight. After this time, the THF was removed in vacuo. The residue was washed through a plug of Celite with hexanes, providing a red solid after removal of the solvent in vacuo. This residue was then dissolved in 3.2 mL CH₂CI_2, after which Me₃SiCI (0.12 mL, 0.980 mmol, 3.0 eq.) was added. The reaction mixture was stirred magnetically for 12 h, then the volatiles were removed in vacuo. The dark residue was added to a small pipet packed with Celite and filtered through using CH₂CI₂. Removal of solvent in vacuo, then washing/decanting the resultant purple solid with pentanes (x3) provided 11 a (130 mg, 47% yield) as a purple solid. Crystals suitable for X-ray diffraction were grown by vial-in- vial solvent diffusion of a concentrated solution of 11a in CH₂CI₂ with hexanes. ¹H-NMR (400 MHz, C₆D₆) δ 7.47 (dd, J = 6.4, 2.9 Hz, 4H), 7.01 (dd, J = 6.4, 2.9 Hz, 4H), 5.65 (s, 4H), 2.19 (t, J = 7.4 Hz, 4H), 1.59 - 1.34 (m, 4H), 0.86 (t, J = 7.3 Hz, 6H). ¹³C-NMR (101 MHz, C₆D₆) δ 142.37, 133.49, 127.81 , 125.71 , 125.34, 1 14.60, 109.56, 33.16, 21.40, 13.99. Analysis Calcd for C₂₆H₂₆CI₂Ti (457.26): HC, 68.29; H, 5.73; Found: C, 68.15; H, 5.88.

Example IX

Synthesis of

(9b)

In the glovebox, under N₂ atmosphere, a vial was charged with 9-(di(1 /- -inden-2- yl)methylene)fluorene (6) (92 mg, 0.226 mmol, 1.0 eq.) and 4.5 mL THF. The mixture was stirred magnetically and cooled to -35 °C, after which time solid NaHMDS (91.3 mg, 0.498 mmol, 2.2 eq.) was added in one portion; the reaction mixture immediately went to a deep purple color. The reaction was allowed to warm slowly to ambient temperature and stirred for a total time of 5 h. The homogenous solution was then cooled back to -35 °C and solid (Me₂N)₂ZrCI₂ · DME (81 mg, 0.237 mmol, 1.05 eq.) was added. The reaction mixture was allowed to warm slowly to ambient temperature and stirred overnight. After this time, the THF was removed in vacuo. The brown residue was filtered through Celite with PhH and concentrated. The resulting solid was dissolved in 2.3 mL CH₂CI_2, after which Me₃SiCI (0.09 mL, 0.86 mmol, 3.0 eq.) was added. The reaction mixture was stirred magnetically at ambient temperature for 12 h, during which time red precipitates crash out. The volatiles were removed in vacuo, and the residue washed with 2 mL Et₂0, then 6 mL hexanes. The supernatant was decanted off, and the residue washed with further 6 mL portions of hexanes (x3) to provide, after removal of trace solvent in vacuo, the desired 9b (1 14 mg, 89% yield) as an orange, highly insoluble solid. Crystals suitable for X-ray diffraction were grown by slow precipitation of a PhMe/PhH solution. ¹H-NMR (400 MHz, C₆D₆) δ 7.60 (d, J = 7.7 Hz, 2H), 7.53 (d, J = 7.6 Hz, 2H) 7.50 (dd, J = 6.5, 3.1 Hz, 4H), 7.16 (dt, J = 1 .0, 7.6 Hz), 6.97 (dd, J = 3.1 , 6.5 Hz, 4H), 6.88 (dt, J = 1 .1 , 7.6 Hz, 2H), 5.68 (s, 4H). ¹³C-NMR (100 MHz, C₆D₆) 5 141 .3, 137.4, 129.5, 129.2, 128.5, 127.6, 127.1 , 126.9, 125.3, 125.0, 120.3, 1 16.6, 101.7. Analysis Calc'd for C₃₂H₂₂CI₂Zr · C₆H₅CI (681 .20 g/mol): C, 67.20; H, 3.71 ; Found: C, 66.90; H, 4.07.

Example X

Synthesis of Ph₂C=C(C₉H₆)2ZrCl2 (10b)

In the glovebox, under N₂ atmosphere, a vial was charged with 2,2'-(2,2-diphenylethene- 1 , 1 -diyl)bis(1 H-indene) (7) (255 mg, 0.624 mmol, 1 .0 eq.) and 12.5 mL THF. The mixture was stirred magnetically and cooled to -35 °C, after which time solid NaHMDS (252 mg, 1.37 mmol, 2.2 eq.) was added in one portion; the reaction mixture immediately took on a deep red coloration. The reaction was allowed to warm slowly to ambient temperature and stirred for a total time of 5.5 h. The homogenous solution was then cooled back to -35 °C and solid (Me₂N)₂ZrCI₂ · DME (223 mg, 0.655 mmol, 1 .05 eq.) was added. The reaction mixture was allowed to warm slowly to ambient temperature and stirred overnight. After this time, the THF was removed in vacuo. The residue was filtered through Celite with PhH and concentrated. The resultant residue was dissolved in 3 mL CH₂CI_2, after which Me₃SiCI (0.28 mL, 1.87 mmol, 3.0 eq.) was added. The reaction mixture was stirred magnetically for 12 h, then the volatiles were removed in vacuo. The resulting residue was dissolved in CH₂CI₂, after which time slow addition of hexanes causes precipitation of the desired complex. The supernatant was decanted, and the procedure repeated, to give 10b (200 mg, 56%) as a yellow powder. Crystals suitable for X-ray diffraction were grown by layering a concentrated solution of 10b in CH₂CI₂ with pentane. ¹H-NMR (400 MHz, C₆D₆) δ 7.57 - 7.47 (m, 4H), 7.39 (dd, J = 6.5, 3.1 Hz, 4H), 7.10 - 6.93 (m, 6H), 6.90 (dd, J = 6.5, 3.1 Hz, 4H), 5.62 (s, 4H). ¹³C-NMR (100 MHz, C₆D₆) δ 144.39, 139.64, 130.27, 128.67, 128.54, 128.51 , 128.26 (found by gHMBC) 126.57, 124.86, 1 17.73, 102.64. Analysis Calcd for C₃₂H₂₂CI₂-C₆H₅CI (681 .20): C, 67.00; H, 4.00; Found: C, 67.19; H, 4.38.

Example XI

Synthesis of n-Pr₂C=C(C₉H₆)₂ZrCI₂ (11 b) In the glovebox, under N₂ atmosphere, a vial was charged with 2,2'-(2-propylpent-1 -ene- 1 , 1 -diyl)bis(1 H-indene) (8) (130 mg, 0.382 mmol, 1 .0 eq.) and 7.6 mL THF. The mixture was stirred magnetically and cooled to -35 °C, after which time solid NaHMDS (147 mg, 0.802 mmol, 2.1 eq.) was added in one portion. The reaction was allowed to warm slowly to ambient temperature and stirred for a total time of 5.5 h. The homogenous solution was then cooled back to -35 °C and solid (Me₂N)₂ZrCI₂ · DME (137 mg, 0.401 mmol, 1 .05 eq.) was added. The reaction mixture was allowed to warm slowly to ambient temperature and stirred overnight. After this time, the THF was removed in vacuo. The residue was filtered through Celite with pentanes and the solvent removed in vacuo. The resultant

green/yellow residue was dissolved in 3.7 mL CH₂CI_2, after which trimethylsilylchloride

(0.14 mL, 1.1 mmol, 3.0 eq.) was added. The reaction mixture was stirred magnetically for 12 h, then the volatiles were removed in vacuo. The orange residue was washed with 5:1 pentane/Et₂0 to remove impurities, then filtered through Celite with PhH and concentrated to provide 11 b as a yellow solid (155 mg, 81 % yield). ¹H-NMR (400 MHz, C₆D₆) δ 7.47 (dd, J = 6.5, 3.1 Hz, 4H), 6.97 (dd, J = 6.5, 3.1 Hz, 4H), 5.57 (s, 4H), 2.24 - 2.15 (m, 4H), 1 .59 - 1.35 (m, 4H), 0.86 (t, J = 7.4 Hz, 6H). ¹³C-NMR (101 MHz, C₆D₆) δ 143.01 , 129.08, 126.53, 125.70, 124.88, 1 18.16, 102.54, 33.09, 21.47, 13.98. Analysis Calcd for

C₂₆H₂₆CI₂Zr (500.61 ): C, 62.38; H, 5.23; Found: C, 62.23; H, 5.41 . Example XII

Comparative examples

The following known metallocene complexes were used for the comparative

polymerization examples:

A biphenyl bis(2-indenyl)zirconium dichloride B 1 ,2-Ethylene bis(9-fluorenyl)zirconium dichloride C rac-Ethylene bis(indenyl)zirconium dichloride

D rac- 1 ,2-Ethylene bis(4,5,6, 7-tetrahydro- 1 -indenyl)zirconium dichloride

E rac-dimethylsily bis(tetrahydro- 1 -indenyl)zirconium dichloride Polymerization of Homogeneous Catalysts: around 1 mg of each complexes 9a, 10a, 11a, 9b, 10b, A, B, C, D and E was suspended in 5 ml toluene. Methylalumoxane (10% in toluene, M:AI = 1 :1500) was added to the suspended complex in toluene. After around two minutes shaking, the mixture was transferred under inert atmosphere to a 2 liter autoclave reactor filled with 250 ml of /sopentane, 100 ml of 1 -hexene, and thermostated at 60^° C. An ethylene pressure of 20 bar was applied for 1 hour. After releasing the pressure, the polymer was filtered through an airless filter funnel, washed with diluted hydrochloric acid, water and acetone, and finally dried in vacuum. The polymerization results are presented in Table 1.

Polymerization Supported Catalysts: In a round bottom flask, 1 ml of Methylalumoxane (MAO) (10% in toluene) was added to the mixture of one gram of dry silica with 20 ml of toluene to afford the treated silica with MAO. In a separate flask, around 2.5 mg of each complexes 9a, 10a, 11 a, 9b, 10b was suspended in 5 ml toluene. Methylalumoxane (10% in toluene, M:AI = 1 :1000) was added to the suspended complex in toluene to yield the activated catalyst. After around two minutes shaking, the mixture contains the active catalyst was transferred under inert atmosphere to the flask contains the treated silica and stirring at 50° C for about an hour then dry the mixture under vacuum to afford the supported catalysts S-9a, S-10a, S-11 a, S-9b, and S-10b. Around 0.2 gram of each catalyst S-9a, S-10a, S-11a, S-9b, or S-10b was transferred under inert atmosphere to a 2 liter autoclave reactor filled with 250 ml of /sopentane, 100 ml of 1 -hexene, and thermostated at 87^°C. An ethylene pressure of 20 bar was applied for 1 hour. After releasing the pressure, the polymer was filtered through an airless filter funnel, washed with diluted hydrochloric acid, water and acetone, and finally dried in vacuum. The polymerization results are presented in Table 2.

1 -Hexene Copolymer Quantification: ¹³C-NMR analysis was performed at 130 °C on a Bruker 400 MHz NMR spectrometer. Polyethylene samples of 250 mg were kept in a sample vial and dissolved in o-dichlorobenzene (ODCB) at 130°C. The DMSO-d₆ was used as an internal lock having concentration 3:97 (v/v) with ODCB solvent. The acquired data were processed and analyzed using XWINNMR software version 3.5.

Gel Permeation Chromatography (GPC): measurements were performed using Waters Alliance GPC 2000 instrument. The Polyethylene samples were dissolved in 1 ,2,4- trichlorobenzene (flow rate 1 ml/min) and measured at 150 °C.

Density analysis: The density of the polyethylene samples was measured using a Tyoceiki automatic densitometer model DH-100.

Differential scanning calorimetry (DSC): The DSC test of the polyethylene sampl performed using TA Instruments Model Q2000 & Q1000.

Table 1. The polymerization results of the homogeneous catalysts

ND=not determined Table 2. The polymerization results of the supported catalysts

Discussion The above experiments show that with the use of the metallocene complexes according to the invention LLDPE can be obtained with a high weight average molecular weight and a high amount of branches per 1000 C atoms.

Scheme 1 , Process for the preparation of metallocene complexes

Ti- 11a, 81% Zr: 11 b, 37%

Claims

1. Metallocene complex according to the following formula (1 )

M is titanium, zirconium, or hafnium and

2. Metallocene complex according to claim 1 , wherein R-i and R₂ are selected from methyl, ethyl, n-propyl, n-butyl, n-pentyl, n-hexyl, phenyl, 1 -indenyl, 2-indenyl or R-i and R₂ form a ring together with the carbon atom to which they are bound to form a 5 or 6-membered ring which may be substituted or unsubstituted.

3. Metallocene complex according to claim 1 or 2, wherein Ri and R₂ are the same.

4. Metallocene complex according to anyone of claims 1 -3, wherein R-i and R₂ are chosen from n-propyl, n-butyl, n-pentyl and n-hexyl.

5. Metallocene complex according to anyone of claims 1 -4, wherein M is Ti.

6. Metallocene complex according to anyone of claims 1 -5, wherein Xi and X₂ are CI.

7. Composition comprising the metallocene complex according to anyone of claims 1 -6, wherein the metallocene complex is present on a support.

8. Process for the preparation of a metallocene complex according to anyone of claims 1- 6, comprising the steps of

a. transforming 2-bromoindene to the corresponding Grignard reagent 2-indeneMgBr b. reacting 2-indeneMgBr with tri-n-butylchloride to give (2-C₉H₇)Mg(n-butyl)₃

c. reacting (2-C₉H₇)Mg(n-butyl)₃ with

R₂ under Pd catalyzed conditions to form ligand precursors,

d. creating anions of the ligand precursors with natriumhexametyldisiloxane

9. Process for the preparation of olefin polymers by polymerizing one or more olefins in the presence of the metallocene complex of any one of claims 1 -6 or in the presence of the composition of claim 7 and a cocatalyst.

10. Process according to claim 9, wherein at least one olefin is ethylene.

1 1. Process according to claim 9 or claim 10, wherein a mixture of ethylene and at least one other olefin is used.

12. Process according to claim 1 1 , wherein the other olefin is chosen from 1 -butene, 1- hexene or 1 -octene.

13. Process according to any one of claims 9-12, wherein an organoaluminum cocatalyst is present.

14. Polyolefin, preferably polyethylene, more preferably linear low density polyethylene obtainable by the process of any one of claims 9-13.

15. Polyolefin according to claim 14, wherein the amount of branches per 1000 carbon atoms as determined using ¹³C NMR is at least 18.