WO2008061900A1

WO2008061900A1 - Polymerisation of ethylene and alpha olefins with single site catalysts having an anionic scorpion-like ligand

Info

Publication number: WO2008061900A1
Application number: PCT/EP2007/062111
Authority: WO
Inventors: Guillaume Michaud; Caroline Hillairet; Sabine Sirol
Original assignee: Total Petrochemicals Research Feluy SA
Current assignee: Total Petrochemicals Research Feluy SA
Priority date: 2006-11-24
Filing date: 2007-11-09
Publication date: 2008-05-29
Anticipated expiration: 2009-05-24
Also published as: US20100298122A1; EP2089399B1; EP1925620A1; EP2089399A1

Abstract

The present invention discloses single site catalyst systems having anionic scorpion-like three dimensional structure, that are suitable for oligomerising or polymerising ethylene and alpha-olefins.

Description

POLYMERISATION OF ETHYLENE AND ALPHA OLEFINS WITH SINGLE SITE CATALYSTS HAVING AN ANIONIC SCORPION-LIKE LIGAND

The present invention related to the field of single site catalyst systems having anionic scorpion-like three dimensional structure that are suitable for oligomerising or polymerising ethylene and alpha-olefins.

There exists a multitude of catalyst systems available for polymerising or oligomerising ethylene and alpha-olefins, but there is a growing need for finding new systems capable to tailor polymers with very specific properties. More and more post- metallocene catalyst components based on early or late transition metals from Groups 3 to 10 of the Periodic Table have recently been investigated such as for example those disclosed in Gibson and al. review (Gibson, V.C.; Spitzmesser, S. K., Chem. Rev. 2003, 103, p. 283). But there is still a need to improve either the specificities or the performances of these systems.

It is an aim of the present invention to provide a new single site catalyst component based on beta-diimine ligands with a chelating pendant arm.

It is also an aim of the present invention to provide single site catalyst components having a scorpion-like spatial organisation.

It is another aim of the present invention to provide active catalyst systems based on these catalyst components.

It is a further aim of the present invention to provide a process for polymerising or for oligomerising ethylene and alpha-olefins with these new catalyst systems.

It is yet a further aim of the present invention to provide a polyethylene by polymerising ethylene with these new catalyst systems. Accordingly, the present invention discloses a ligand of general formula I,

wherein R1 , R2, R3, R4, R6, R7, R8, R9 and R10 are each independently selected from hydrogen, unsubstituted or substituted hydrocarbyl, or inert functional group, wherein two or more of those groups can be linked together to form one or more rings, with the restriction that R1 and R3 and/or R2 and R4 and/or R9 and R10, cannot be simultaneously oxazoline, wherein Z is selected from groups 15 or 16 of the Periodic Table and wherein m is the valence of Z minus one.

By inert functional group, is meant a group, other than hydrocarbyl or substituted hydrocarbyl, that is inert under the complexation conditions to which the compound containing said group is subjected. They can be selected for example from halo, ester, ether, amino, imino, nitro, cyano, carboxyl, phosphate, phosphonite, phosphine, phosphinite, thioether and amide. Preferably, they are selected from halo, such as chloro, bromo, fluoro and iodo, or ether of formula - OR^* wherein R^* is unsubstituted or substituted hydrocarbyl. After metallation of the ligand, an inert functional group must not coordinate to the metal more strongly than the groups organised to coordinate to the metal and thereby displace the desired coordinating group. Ligand I results from the reaction between a beta-diimine Il and a compound of formula III wherein X is a leaving group, preferably halogen for example Br.

wherein R5 is hydrogen.

Preferably, R1 and R2 are the same or different and are unsubstituted or substituted alkyl groups, unsubstituted or substituted aryl groups, or unsubstituted or substituted cycloalkyl groups, more preferably, they are unsubstituted or substituted phenyl groups and if they are substituted, the substituents may be joined to form a closed structure. If the phenyls are substituted, the substituents preferably occupy 2 and 6 positions.

Preferably, R3 and R4 are the same or different, hydrogen, unsubstituted or substituted alkyl groups, unsubstituted or substituted aryl groups, or unsubstituted or substituted cycloalkyl groups, more preferably, they are unsubstituted or substituted alkyl groups. Optionally R3 and R4 may also be linked together to form a cyclohexyl ring.

In another embodiment according to the present invention, R1 with R3 and/or R2 with R4 are linked together to form a ring.

Preferably, Z is selected from N, P, O or S.

Preferably, R6, R7, R8, R9 and R10 are the same or different, hydrogen, unsubstituted or substituted alkyl groups, unsubstituted or substituted aryl groups, or unsubstituted or substituted cycloalkyl groups. R8 and R9 and/or R9 and R10 can be linked together to form a ring, for example a pyridine, a quinoline, an isoquinoline, a pyrrolyl, a furyl or a thiophenyl group.

Examples of formula III include 2-(bromomethyl)-5-nitrofuran, 2-(bromomethyl)-1 ,3- dioxalane, 2-(bromomethyl)tetrahydro-2H-pyran, 2-(bromomethyl)-5- thfluoromethyl)furan, 3(-bromomethyl)pyridazine, 2-bromomethylpyridine, 1 -bromo- 2-ethoxyethane, 2-bromoethylacetate, 1-bromo-2-(2-methoxyethoxy)ethane, [(2- bromoethoxy)methyl]benzene and 3-(bromomethyl)-2,4,10-thoxaadamantane, 2- bromo-N,N-dimethylaniline.

The invention also discloses a catalyst component of formula IV:

IV

resulting from the complexation of deprotonated ligand I with the metallic salt MX'_n+i in a solvent, wherein M is a metal Group 3 to 10 of the periodic Table, wherein X' is the same or different and can be a halogen, alcoholate, or substituted or unsubstituted hydrocarbyl, wherein n+1 is the valence of M and wherein said ligand I is deprotonated by a base and characterised in that pending arm

is folding to coordinate heteroatom Z to metal M. The base used for deprotonating ligand I can be selected for example from butyl lithium, methyl lithium, sodium hydride. More preferably it is butyl lithium.

Preferably, M is Ti, Zr, Hf, V, Cr, Mn, Fe, Co, Ni, Pd or rare earths. More preferably, it is Cr or Ti.

Preferably, X' is halogen, more preferably it is chlorine.

The metal is complexed with the two nitrogen atoms of the starting beta-diimine and during the complexation reaction, the complex folds around in order to coordinate heteroatom Z to the metal to form a three dimensional scorpion-like structure.

The solvent may be selected from dichloromethane or tetrahydrofuran and the complexation reaction is carried out at room temperature.

The present invention also discloses an active catalyst system comprising the single site catalyst component of formula IV and an activating agent having an ionising action.

Suitable activating agents are well known in the art. The activating agent can be an aluminium alkyl represented by formula AIR⁺ _nX3_-n wherein R⁺ is an alkyl having from 1 to 20 carbon atoms and X is a halogen. The preferred aluminium alkyls are triisobutyl aluminium (TIBAL) or triethyl aluminium (TEAL).

Alternatively, it can be aluminoxane and comprise oligomeric linear and/or cyclic alkyl aluminoxanes represented by formula

R - (AI -O)_n-Al R^*2

R*

for oligomeric, linear aluminoxanes and by formula R*

for oligomeric, cyclic aluminoxane,

wherein n is 1 -40, preferably 1-20, m is 3-40, preferably 3-20 and R^* is a Ci-Cs alkyl group and preferably methyl or isobutyl.

Preferably, the activating agent is selected from methylaluminoxane (MAO) or tetra- isobutyldialuminoxane (IBAO), more preferably, it is MAO.

The amount of activating agent is selected to give an Al/M ratio of from 100 to 3000, preferably of from 500 to 2000. The amount of activating agent depends upon its nature, the preferred Al/M ratio is of about 2000

Suitable boron-containing activating agents may comprise a triphenylcarbenium boronate such as tetrakis-pentafluorophenyl-borato-triphenylcarbenium as described in EP-A-0427696, or those of the general formula [L'-H] + [B An Ar₂ X3 X₄]- as described in EP-A-0277004 (page 6, line 30 to page 7, line 7).

The amount of boron-containing activating agent is selected to give a B/M ratio of from 0.5 to 5, preferably of about 1.

In another embodiment, according to the present invention, the single site catalyst component of formula IV may be deposited on a conventional support. Preferably, the conventional support is silica impregnated with MAO. Alternatively the support may also be an activating support such as fluohnated alumina silica.

The present invention further discloses a method for preparing an active catalyst system that comprises the steps of:

a) providing a beta-diimine ligand precursor of formula II; b) reacting the beta-diimine ligand precursor of formula Il with compound III to obtain a ligand; c) deprotonating the ligand of step b) with a base; d) complexing the deprotonated ligand of step c) with a metallic salt MX'_n+i; e) retrieving a catalyst component of formula IV; f) activating the catalyst component of step e) with an activating agent having an ionising action; g) optionally adding a cocatalyst; h) retrieving an active oligomerisation or polymerisation catalyst system.

Alternatively, in step f) catalyst component IV is deposited on a support impregnated with an activating agent or on an activating support containing fluor.

The cocatalyst may be selected from thethylaluminium, triisobutylaluminum, tris-n- octylaluminium, tetraisobutyldialuminoxane or diethyl zinc.

The active catalyst system is used in the oligomerisation and in the polymerisation of ethylene and alpha-olefins.

The present invention discloses a method for the oligomerisation or the homo- or co- polymerisation of ethylene and alpha-olefins that comprises the steps of: a) injecting the active catalyst system into the reactor; b) injecting the monomer and optional comonomer either before or after or simultaneously with step a); c) maintaining under polymerisation conditions; d) retrieving the oligomers and/or polymer.

The pressure in the reactor can vary from 0.5 to 50 bars, preferably from 5 to 25 bars.

The polymerisation temperature can range from 10 to 100⁰C, preferably from 50 to 85°C. The preferred monomer and optional comonomer can be selected from ethylene, propylene or 1 -hexene. Alternatively, the optional comonomer can be a polar functionalised alpha-olefin.

With a catalyst activated by MAO, the polymer formed is characterised by a melting point comprised between 130 and 135 ⁰C as measured by Differential Scanning Calohmetry (DSC) method. They also have a high weight average molecular weight Mw. The molecular weight distribution is measured by the polydispersity index D defined as the ratio Mw/Mn of the weight average molecular weight Mw over the number average molecular weight Mn. Molecular weights are measured by Gel Permeation Chromatography (GPC)

Examples-

Preparation of catalyst components-

Synthesis of ligand L1.

Step 1.

The beta-diimine was synthesised according to the procedure published by Feldman and al. (Organometallics 1997, 16, p. 1514).

Step 2.

760 mg (3 mmol) of 2-bromomethylpyridine.HBr and 436 mg (3.15 mmol) of potassium carbonate were degassed under vacuum for 1 hour. 10 ml_ of dry acetone were added and the mixture was stirred under argon for 6 hours at room temperature (about 25 ⁰C). The solvent was removed and the 2-bromomethylpyhdine was extracted with 3 x 10 ml_ of diethyl ether under inert atmosphere. The solvent was removed to afford a pink oil with quantitative yield.

Step 3. 1.26 g (3 mmol) of beta-diimine were dissolved in 15 mL of dry THF under argon. The solution was cooled to a temperature of -20⁰C and 2 ml_ (3.15 mmol) of n-BuLi (1.6 M in hexane) were added dropwise. The colourless solution turned immediately bright yellow and was stirred at room temperature for 30 minutes. The solution was cooled to a temperature of -20⁰C and a solution of 2-bromomethylpyhdine in 10 ml_ of dry THF was added by canula. The solution was allowed to warm to room temperature and was stirred overnight, before being heated at a temperature of 80°C for 6 hours under reflux. After that time, the solvent was evaporated to dryness. The residue was extracted with 10 ml_ of dichloromethane and filtered over neutral alumina. The solution was evaporated to afford a yellow oil that was purified by column chromatography (SiO2, pentane:diethyl ether 95:5 to 80:20). 910 mg of the expected product were obtained as pale yellow oil containing isomers 1a and 1 b, with a yield of 60 %.

The isomers were characterised as follows:

C_3SH₄₇N₃

M=509.77 g.mol^"1

¹H NMR (500 MHz, CDCI₃) results:

Isomer 1a: δ = 1.10 (m, 12H₁ CH₃ ZPr), 1.21 (dd, 12H, J=6.8 Hz, CH₃ /Pr), 1.92 (s, 6H,

CH₃CN), 2.53 (sept, 2H, J=6.8 Hz, CH /Pr), 2.60 (sept, 2H, J=6.8 Hz, CH /Pr), 3.65

(d, 2H, J=7.5 Hz, CH₂), 4.70 (t, 1 H, J=7.5 Hz, CH), 7.11 (m, 2H, CH para Ph), 7.17

(br s, 4H, CH meta Ph), 7.22 (m, 1 H, H5 pyr), 7.38 (d, 1 H, J=7.5 Hz, H3 pyr), 7.66

(td, 1 H, J=7.5 Hz, J=1.8 Hz, H4 pyr), 8.66 (d, 1 H, J=5 Hz, H6 pyr).

Isomer 1b: δ = 1.07 (m, 12H₁ CH₃ ZPr), 1.13 (d, 12H, J=6.9 Hz, CH₃ /Pr), 1.78 (s, 6H,

CH₃CN), 3.20 (sept, 4H, J=6.9 Hz, CH /Pr), 4.06 (s, 2H, CH₂), 7.09 (m, 2H, CH para

Ph), 7.13 (m, 4H, CH meta Ph), 7.18 (m, 1 H, H5 pyr), 7.33 (d, 1 H, J=7.8 Hz, H3 pyr),

7.68 (m, 1 H, H4 pyr), 8.61 (d, 1 H, J=5 Hz, H6 pyr). Synthesis of ligand L2

Using the same procedure as that used to prepare ligand 1 (steps 1 , 2 and 3), ligand L2 was obtained with a yield of 61 %.

¹H NMR (500 MHz, CDCI₃) : δ = 1.26 (s, 18H, CH₃ ffiu), 2.00 (s, 6H, CH₃CN), 3.63 (d, 2H, J=7.5 Hz, CH₂), 4.44 (t, 1 H, J=7.5 Hz, CH), 6.25 (d, 2H, J=7.5 Hz), 7.05 (m, 6H), 7.34 (t, 2H, J=7.5 Hz), 7.62 (t, 1 H, J=7.5 Hz), 8.59 (d, 1 H, J=5 H).

Synthesis of ligand L3

Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3), ligand L3 was obtained with a yield of 41 %.

¹H NMR (500 MHz, CDCI₃) : δ = 1.80 (s, 6H, CH₃), δ = 1.84 (s, 12H, CH₃), 2.25 (s, 6H, CH₃), 3.60 (d, 2H, J=7.5 Hz, CH₂), 4.53 (t, 1 H, J=7.5 Hz, CH), 6.90 (s, 4H), 7.1 - 7.25 (m, 1 H), 7.30-7.80 (m, 3H), 8.58 (m, 1 H).

Synthesis of ligand L4

Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3) except that 2-bromomethylquinoline.HCI was used instead of 2- bromomethylpyridine.HBr, ligand L4 was obtained with a yield of 23%.

¹H NMR (300 MHz, CDCI₃) : δ =1.22 (s, 18H, 2^*tBu), 2.10 (s, 6H, 2^*CH₃), 3.86 (d, 2H, J=7.2 Hz, CH₂), 4.68 (t, 1 H, J=7.2 Hz, CH), 6.31 (d, 2H, J=7.5 Hz,2^*CH Ph), 7.05 (m, 4H, 4*CH Ph), 7.35 (d, 2H, J=7.5 Hz, 2*CH Ph), 7.46 (d, 1 H, J=8.4 Hz, CH quin), 7.53 (t, 1 H, J=7.5 Hz, CH quin), 7.72 (t, 1 H, J=7.6 Hz, CH quin), 7.81 (d, 1 H, J=8.1 Hz, CH quin), 809 (d, 2H, J=8.4 Hz, 2*CH quin).

Synthesis of ligand L5

Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3), except that 2-methoxy-5-nitrobenzyl bromide was used instead of 2- bromomethylpyridine.HBr, ligand L5 was obtained with a yield of 57%.

¹H NMR (300 MHz, CDCI₃) : δ =1.29 (s, 18H, 2^*tBu), 1.99 (s, 6H, 2^*CH₃), 3.52 (d, 2H, J=7.5 Hz, CH₂); 4.00 (s, 3H, OCH₃), 4.17 (t, 1 H, J=7.5 Hz, CH), 6.27 (dd, 2H), 7.05 (m, 6H), 7.37 (dd, 2H), 8.20 (s, 1 H).

Synthesis of ligand L6 Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3), ligand L6 was obtained with a yield of 67%.

¹H NMR (300 MHz, CDCI₃) : δ = 1.98 (s, 6H, CH₃), 3.52 (d, 2H, J=7.5 Hz, CH₂), 4.27 (t, 1 H, J=7.5 Hz, CH), 7.03 (s, 4H), 7.21 (m, 1 H), 7.28 (d, 1 H, J=7.8 Hz), 7.68 (t, 1 H, J=7.6 Hz), 8.61 (m, 1 H).

Synthesis of ligand L7

Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3), ligand L7 was obtained with a yield of 40%.

¹H NMR (300 MHz, CDCI₃) : δ = 1 ,94 (s, 6H, CH₃) ; 3,56 (d, 2H, d, J=7.5 Hz, CH₂) ; 4,42 (t, 1 H, t, J=7.5 Hz, CH) ; 6,68 (t, J_HF=8.3 Hz, 4H) ; 7,14 (m, 1 H), 7,26 (d, 1 H, J=7.5 Hz), 7,61 (t, 1 H, J=7.7 Hz), 8,56 (d, 1 H, J=3.9 Hz).

Synthesis of ligand L8 Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3), ligand L8 was obtained with a yield of 46%.

¹H NMR (300 MHz, CDCI₃) : δ = 1.99 (s, 6H, CH₃), 3.56 (d, 2H, J=7.5 Hz, CH₂), 4.53 (t, 1 H, J=7.5 Hz, CH), 7.18 (m, 1 H), 7.26 (d, 1 H, J=7.8 Hz), 7.65 (t, 1 H, J=7.5 Hz), 8.56 (m, 1 H).

Synthesis of ligand L9

Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3), ligand L9 was obtained with a yield of 69%.

¹H NMR (300 MHz, CDCI₃) : δ = 2.00 (s, 6H, CH₃), 3.65 (d, 2H, J=7.8 Hz, CH₂), 4.67 (t, 1 H, J=7.8 Hz, CH), 6.92 (t, 2H, J=8.1 Hz), 7.14 (m, 1 H), 7.26 (m, 4H), 7.28 (m, 1 H), 7.61 (t, 1 H, J=7.6 Hz), 8.60 (m, 1 H).

Synthesis of ligand L10 Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3), ligand L10 was obtained with a yield of 39%.

¹H NMR (300 MHz, CDCI₃) : δ = 1 ,25 (s, 18H, tBu), 2,05 (s, 6H, CH₃), 2,27 (s, 3H, CH₃ pyr), 2,31 (s, 3H, CH₃ pyr), 3,56 (d, 2H, J=7.2 Hz, CH₂), 3,75 (s, 3H, OCH₃), 4,58 (t, 1 H, J=7.2 Hz, CH), 6,33 (d, J=7.6 Hz, 2H), 7,01 (t, J=7.5 Hz, 2H), 7,10 (t, J=7.4 Hz, 2H), 7,35 (d, J=7.8 Hz, 2H), 8,21 (s, 1 H).

Synthesis of ligand L11

Using the same procedure as that used to prepare ligand L1 (steps 1 , 2 and 3), ligand L11 was obtained with a yield of 76%.

¹H NMR (300 MHz, CDCI₃) : δ = 1 ,37 (s, 18H, tBu), 1 ,97 (s, 6H, CH₃), 2,41 (q, 2H, J=6.6 Hz, CH₂), 3,42 (s, 3H, OCH₃), 3,62 (t, 2H, J=6.4 Hz, CH₂O), 3,77 (t, 1 H, J=7.1 Hz, CH), 6,41 (d, 2H, J=7.6 Hz), 7,04 (t, 2H, J=7.5 Hz), 7,14 (t, 2H, J=7.5 Hz), 7,38 (d, 2H, J=7.8 Hz). Method 1 Preparation of Cr(III) complexes

0.5 mmol of the appropriate ligand were dissolved in 5 ml_ of tetrahydrofuran. 0.5 mmol of n-butyl lithium were added dropwise at a temperature of -15°C. The solution was allowed to warm to room temperature and was stirred for 30 minutes. The solution was added dropwise to a solution of 0.5 mmol of chromium (III) chloride tetrahydrofuran complex dissolved in 5 ml_ of dry tetrahydrofuran. The mixture was stirred under argon overnight at room temperature. The solution was concentrated to approximately 2 ml_ and 10 ml_ of pentane were added. The solid was filtered off, washed twice with 5 ml_ of pentane and dried under vacuum.

Method 2: Preparation of Ti(IV) complexes

0.35 mmol of the appropriate ligand were dissolved in 5 ml_ of tetrahydrofuran. 0.35 mmol of n-butyl lithium were added dropwise at a temperature of -78°C. The solution was allowed to warm to room temperature and was stirred for 30 minutes. The solution was added dropwise to a solution of 0.35 mmol of titanium (IV) tetrachloride dissolved in 5 ml_ of dry tetrahydrofuran cooled at a temperature of -78°C. The mixture was stirred under argon overnight at room temperature. The solution was concentrated to approximately 2 ml_ and 10 ml_ of pentane were added. The solid was filtered off, washed twice with 10 ml_ of pentane and dried under vacuum.

Method 3: Preparation of Zr(IV) complexes

0.35 mmol of the appropriate ligand were dissolved in 5 ml_ of tetrahydrofuran. 0.35 mmol of n-butyl lithium were added dropwise at a temperature of -78°C. The solution was allowed to warm to room temperature and was stirred for 30 minutes. The solution was added dropwise to a solution of 0.35 mmol of zirconium (IV) tetrachloride dissolved in 5 ml_ of dry tetrahydrofuran cooled at a temperature of - 78°C. The mixture was stirred under argon overnight at 70⁰C. The solution was concentrated to approximately 2 ml_ and 10 ml_ of pentane were added. The solid was filtered off, washed twice with 10 ml_ of pentane and dried under vacuum.

Method 4: Preparation of V(III) complexes

0.35 mmol of the appropriate ligand were dissolved in 5 ml_ of tetrahydrofuran. 0.35 mmol of n-butyl lithium were added dropwise at a temperature of -78°C. The solution was allowed to warm to room temperature and was stirred for 30 minutes. The solution was added dropwise to a solution of 0.35 mmol of vanadium (III) trichloride tetrahydrofuran complex dissolved in 5 ml_ of dry tetrahydrofuran cooled at a temperature of -78°C. The mixture was stirred under argon overnight at room temperature. The solution was concentrated to approximately 2 ml_ and 10 ml_ of pentane were added. The solid was filtered off, washed twice with 10 ml_ of pentane and dried under vacuum.

Method 5: Preparation of Fe(III) complexes

0.35 mmol of the appropriate ligand were dissolved in 5 ml_ of tetrahydrofuran. 0.35 mmol of n-butyl lithium were added dropwise at a temperature of -20⁰C. The solution was allowed to warm to room temperature and was stirred for 30 minutes. The solution was added dropwise to a solution of 0.35 mmol of iron (III) trichloride dissolved in 5 ml_ of dry tetrahydrofuran cooled at a temperature of -20⁰C. The mixture was stirred under argon overnight at room temperature. The solution was concentrated to approximately 2 ml_ and 10 ml_ of pentane were added. The solid was filtered off, washed twice with 10 ml_ of pentane and dried under vacuum.

Using method 1 , Cr(III) complex 1 was obtained as a pale grey solid with a yield of 74%.

Using method 1 , Cr(III) complex 2 was obtained as a pale green solid with a yield of 75%.

Using method 1 , Cr(III) complex 3 was obtained as a pale green solid with a yield of 48%.

Using method 2, Ti(IV) complex 4 was obtained as a brown solid with a yield of 94%.

Using method 2, Ti(IV) complex 5 was obtained as a brown solid with a yield of 94%.

Using method 2, Ti(IV) complex 6 was obtained as a brown solid with a yield of 75%.

Using method 1 , Cr(III) complex 7 was obtained.

Using method 2, Ti(IV) complex 8 was obtained as a orange solid with a yield of 56%.

Using method 3, Zr(IV) complex 9 was obtained.

Using method 4, V(III) complex 10 was obtained as a green solid with a yield of 76%.

Using method 5, Fe(III) complex 11 was obtained as a brown solid with a yield of 63%.

11

Using method 1 , Cr(III) complex 12 was obtained as a green solid with a yield of

34%.

12

Using method 2, Ti(IV) complex 13 was obtained as a dark brown solid with a yield of

50%.

Using method 2, Ti(IV) complex 14 was obtained as a clear brown solid with a yield of 70%.

14

Using method 2, Ti(IV) complex 15 was obtained as a black solid with a yield of 44%.

15

Using method 2, Ti(IV) complex 16 was obtained as a red solid with a yield of 19%.

16

Using method 2, Ti(IV) complex 17 was obtained as a yellow solid with a yield of 81 %.

17

Using method 2, Ti(IV) complex 18 was obtained as an orange solid with a yield of 34%.

18

Using method 2, Ti(IV) complex 19 was obtained as a clear brown-orange solid with a yield of 52%.

19

Using method 3, Zr(IV) complex 20 was obtained as a yellow solid with a yield of 63%.

20

High pressure polymerisation of ethylene.

Ethylene polymerisation reactions were performed in a 20 ml_ stainless steel autoclave containing a glass insert, fitted with mechanical stirring, external thermocouple and pressure gauge and controlled by computer. In a typical reaction run, 4 ml_ of dry solvent (toluene or n-heptane) were introduced into the reactor and the temperature and ethylene pressure were raised to the desired values. Ethylene was fed continuously. In an argon-filled glove box, about 5 μmol of the appropriate catalyst were weighted. It was activated with methylaluminoxane (MAO 30 % wt in toluene) in an amount appropriate to obtain a ratio [AI]:[M] of 2000 and it was diluted with toluene to a final volume of 2 ml_. 200 μl_ of the solution of activated catalyst were placed inside the reactor. The injection loop was rinsed with 800 μl_ of solvent. After 1 hour or after an ethylene consumption of 12 mmol, the reaction was quenched with isopropanol and an aliquot was analysed by gas chromatography. The gas chromatographic analysis of the reaction products were performed on a Trace GC apparatus with a Petrocol capillary column (methyl silicone, 100 m long, i.d. 0.25 mm and film thickness of 0.5 μm) working at a temperature of 35°C for 15 min and then heated to a temperature of 250 ⁰C at a heating rate of 5°C/min. The remaining reaction mixture was quenched with MeOH / HCI and the polymer was filtered, washed with methanol and dried at a temperature of 50⁰C, under vacuum, for a period of time of 24 hours.

The results are displayed in Table I and in Table II. TABLE I. Results with the Cr(III) complexes

m PE Activity DSC

Run Complex P (bar) T (⁰C) (mg) (kg/mol/h) Tm (⁰C) ΔH (J.g ¹)

1 1 15 50 47 93 165.5 2 2 15 50 45 86 178.5 3 3 15 50 40 78 177.8

4 7 15 50 36 70 130 170.9

5 12 15 50 41 81 131 170.6

6 1 19 80 27 53 131 202.5

7 2 19 80 26 52 131 209.1

8 3 19 80 32 63 130 183.5

All reactions were performed with 0.5 μmol of catalyst dissolved in 5 ml_ of n-heptane during 1 hour.

MAO was added to give a [AI]:[Cr] ratio of 2000.

Activities are expressed in kg of polyethylene per mol Cr per hour.

TABLE II. Results with the Ti(IV) complexes

Time m PE Activity

Run Complex P (bar) DSC

T (⁰C) (min) (mg) (kg/mol/h) Tm (⁰C) ΔH (J.g ¹)

9 4 15 50 60 552 1111 135 133,3

10 5 15 50 60 630 1198 135 122,1

1 1 6 15 50 60 583 1027 133 138,6

12 4 19 80 51 812 1909 134 136,9

13 5 19 80 48 862 2094 135 145,7

14 6 19 80 52 955 2187 136 150,4

15 8 19 80 60 257 512 134 120.0

16 13 19 80 60 274 549 134 125.0

17 14 19 80 60 408 1646 136 108.2

18 15 19 80 60 301 1209 139 119.1

19 16 19 80 60 705 1399 132 98.7

20 17 19 80 60 387 765 133 129.7

21 18 19 80 60 260 514 133 96.6

22 19 19 80 60 383 749 138 109.2

MAO was added to give a [AI]:[Ti] ratio of 2000. Activities are expressed in kg of polyethylene per mol Ti per hour.

TABLE III. Results with the Zr(IV) complex

Run Con^ P _(ba_r) T fC, ^ , *£» , _Tm ,_χ, "^ ,,,-,,

23 9 15 50 395 778 133 130.1

24 9 19 80 473 932 134 148.9

25 20 19 80 249 480 138 137.7

MAO was added to give a [AI]:[Zr] ratio of 2000.

Activities are expressed in kg of polyethylene per mol Zr per hour.

TABLE IV. Results with the V(III) complex

Run Convex P,_bar, T₁-C, ^ ,*£», " ,

25 10 15 50 52 103 133 139.1 27 10 19 80 63 125 133 146.8

MAO was added to give a [AI]:[V] ratio of 2000.

Activities are expressed in kg of polyethylene per mol V per hour.

Polymerisation of ethylene with a supported catalyst

Complex 5 was deposited on a MAO impregnated silica (Sylopol 952X1836), with 2 wt % of complex based on the total weight of the obtained supported catalyst. This supported catalyst was used for the polymerisation of ethylene. Ethylene polymerisation reactions were carried out in a 130 ml stainless steel autoclave equipped with mechanical stirring and a stainless steel injection cylinder. In a typical reaction run, the reactor was first dried under nitrogen flow at 100⁰C during 10 min. Then it was cooled down to the reaction temperature (85°C) and 35 ml of isobutane were introduced into the reactor with a syringe pump. The pressure was adjusted to the desired value (23.8 bar) with ethylene. In an argon-filled glove box, 301 mg of the supported catalyst, 0.6 ml of TiBAI and 0.5 ml of n-heptane were placed into the injection cylinder. The valve was closed and the cylinder was connected to the reactor under nitrogen flow. The active catalyst mixture was then introduced into the reactor with 40 ml of isobutane. After 1 hour at 750 rpm, the reactor was cooled down to room temperature and slowly depressurised. The polymer was recovered and characterised by DSC. The polymerisation results are displayed in Table V.

TABLE V: Polymerisation results with supported Ti(IV) complex 5

^* Activity is expressed as g of polyethylene per g of supported catalyst per hour.

Due to the high molecular weight of the obtained polymers, GPC and ¹³C NMR analysis were not possible, even in TCB at 135°C.

Claims

CLAIMS.

1. A deprotonated ligand of general formula I,

wherein R1 , R2, R3, R4, R6, R7, R8, R9 and R10 are each independently selected from hydrogen, unsubstituted or substituted hydrocarbyl, or inert functional group and wherein two or more of said R's can be linked together to form one or more rings, with the restriction that R1 and R3, R2 and R4, and R9 and R10, cannot all be simultaneously oxazoline, wherein Z is selected from groups 15 or 16 of the Periodic Table and m is the valence of Z minus one.

2. The deprotonated ligand of claim 1 wherein R1 and R2 are the same or different and are unsubstituted or substituted alkyl groups, unsubstituted or substituted aryl groups, or unsubstituted or substituted cycloalkyl groups.

3. The deprotonated ligand of claim 2 wherein R1 and R2 are the same and are unsubstituted or substituted phenyl groups.

4. The deprotonated ligand of any one of claims 1 to 3 wherein R3 and R4 are the same or different, and are hydrogen, unsubstituted or substituted alkyl groups, unsubstituted or substituted aryl groups, or unsubstituted or substituted cycloalkyl groups.

5. The deprotonated ligand of claim 4 wherein R3 and R4 are unsubstituted or substituted alkyl groups or are linked together to form a cyclohexyl ring.

6. The deprotonated ligand of any one of the preceding claims wherein R1 with R3 and/or R2 with R4 are linked together to form a ring.

7. The deprotonated ligand of any one of the preceding claims wherein Z is selected from N, P, O or S.

8. The deprotonated ligand of any one of the preceding claims wherein R6, R7, R8, R9 and R10 are the same or different, and are hydrogen, unsubstituted or substituted alkyl groups, unsubstituted or substituted aryl groups, or unsubstituted or substituted cycloalkyl groups.

9. A catalyst component of formula IV:

IV

resulting from the complexation of deprotonated ligand I of any one of claims 1 to 9 with the metallic salt MX'_n+i in a solvent, wherein M is a metal Group 3 to 10 of the periodic Table, X' is the same or different and is halogen, alcoholate, or substituted or unsubstituted hydrocarbyl and wherein n+1 is the valence of M and characterised in that pending arm

is folding to coordinate heteroatom Z to metal M.

10. The metallic complex of claim 10 wherein M is Ti, Zr, Hf, V, Cr, Mn, Fe, Co, Ni, Pd.

11. An active catalyst system comprising the metallic complex of claim 10 or claim 11 and an activating agent having an ionising action.

12. A method for preparing an active catalysts system that comprises the steps of:

a) providing a beta-diimine ligand precursor of formula II; b) reacting the beta-diimine ligand precursor of formula Il with compound III to obtain a ligand; c) deprotonating the ligand of step b) by subtracting the R5 hydrogen with a base; d) complexing the deprotonated ligand of step c) with a metallic salt

e) retrieving a catalyst component of formula IV; f) activating the catalyst component of step e) with an activating agent having an ionising action; g) optionally adding a cocatalyst; h) retrieving an active oligomerisation or polymerisation catalyst system.

13. A method for the oligomerisation or for the homo- or co-polymerisation of ethylene and alpha-olefins that comprises the steps of: a) injecting the active catalyst system of claim 13 into the reactor; b) injecting the monomer and optional comonomer either before or after or simultaneously with step a); c) maintaining under polymerisation conditions; d) retrieving the oligomers and/or polymer.

14. The method of claim 14 wherein the monomer and optional comonomer are selected from ethylene, propylene and 1 -hexene.