Catalyst component and catalyst system having a high polymerization activity for preparing polymers

Abstract

Catalyst systems having a high polymerization activity comprise at least one catalyst component of the formula (I):

Description

[0001] The present invention relates to catalyst components and catalyst systems having a high polymerization activity for preparing polymers which have a high melting point. The present invention also relates to an economical and environmentally friendly process for preparing polymers having a high melting point.

[0002] DE-A-4332009 discloses a process for preparing organometallic fluorides. Here, organometallic fluorides containing a π system are obtained by reacting a fluorine-free organometallic halide with a tin fluoride of the formula R3SnF, where R are identical or different and are C1-C10-alkyl, C6-C14-aryl, C2-C10-alkenyl, C7-C20-arylalkyl or C7-C15-alkylaryl.

[0003] EP-A-210 615 discloses catalysts for the polymerization of styrene and processes for the polymerization of monostyrene to syndiotactic polystyrene.

[0004] It is known from Macromolecules 21 (1988), 3356 that titanium compounds containing a cyclopentadienyl ring have a particularly high polymerization activity. The styrene polymers obtained using these compounds as catalysts have comparatively low melting points.

[0005] It is an object of the present invention to provide a catalyst component and a catalyst system which has a high polymerization activity and gives polymers having high melting points. A further object of the present invention is to provide an economical and environmentally friendly polymerization process.

[0006] We have found that this object is achieved by a catalyst component for the polymerization of olefins, which comprises at least one compound of the formula (I):

RanM1Rbm  (I),

[0007] where

[0008] M1=Ti, Zr or Hf,

[0009] Ra=C5 (R1, R2, R3, R4, R5) or C6 (R1, R2, R3, R4, R5, R6), where R1, R2, R3, R4, R5 and R6 are identical or different and are each a hydrogen atom, a C1-C20-alkyl group, a C1-C10-alkoxy group, a C1-C10-fluoroalkyl group, a C6-C20-aryl group, a C6-C10-aryloxy group, a C2-C10-alkenyl group, a C6-C10-fluoroaryl group, a C7-C40-arylalkyl group, a C7-C40-alkylaryl group, a C8-C40-arylalkenyl group, a silyl group or a germyl group or adjacent radicals R1, R2, R3, R4, R5 and R6 together with the atoms connecting them form a ring system,

[0010] Rb=a fluorine atom when m=1, at least one fluorine atom when m>1 and can be identical or different and can be at least one hydrogen atom, a C1-C20-alkyl group, a C1-C10-alkoxy group, a C1-C10-fluoroalkyl group, a C6-C20-aryl group, a C6-C10-aryloxy group, a C2-C10-alkenyl group, a C6-C10-fluoroaryl group, a C7-C40-arylalkyl group, a C7-C40-alkylaryl group, a C8-C40-arylalkenyl group, an OH group, an NR72 or SR81 group, where R7 and R8 are each a C1-C20-alkyl group, a C1-C10-alkoxy group, a C1-C10-fluoroalkyl group, a C6-C20-aryl group, a C6-C10-aryloxy group, a C2-C10-alkenyl group, a C6-C10-fluoroaryl group, a C7-C40-arylalkyl group, a C7-C40-alkylaryl group, a C8-C40-arylalkenyl group, a silyl group, a germyl group or a halogen atom, an —OC(O)F group, an —OC(O)CRc3 group, an —OC(O)C5Rd4 group or an —OC(O)C6Re5 group, where Rc, Rd and Re are at least one fluorine atom and Rc, Rd and Re can be identical or different and can be at least one hydrogen atom, a C1-C20-alkyl group, a C1-C10-alkoxy group, a C1-C10-fluoroalkyl group, a C6-C20-aryl group, a C6-C10-aryloxy group, a C2-C10-alkenyl group, a C6-C10-fluoroaryl group, a C7-C40-arylalkyl group, a C7-C40-alkylaryl group, a C8-C40-arylalkenyl group, an OH group, an NR72 or SR8 group, a silyl group, a germyl group or a halogen atom,

[0011] m and n are integers, m+n=2-4 and m is at least 1.

[0012] The present invention has the advantage that these catalyst components give catalyst systems having a high polymerization activity. The polymerization activity of the catalysts of the invention is calculated as the mass of polymer produced, based on the molar amount of the compound of group IV of the Periodic Table and based on the polymerization time. The particular advantage of the present invention is that polymers having high melting points are obtained using catalyst systems having a high polymerization activity. The increase in the polymerization activity in the case of previously known catalyst systems was hitherto associated with the disadvantage that the melting points of the polymers obtained always decreased. The high polymerization activity of the catalyst systems enables a polymerization to be carried out with very good results using smaller amounts of catalyst systems. This makes the polymerization process very economical and environmentally friendly.

[0013] Preference is given to catalysts of the present invention which have a cyclopentadienyl ring as ligand and 3 fluorine atoms bound directly to the metal atom M1. Catalyst systems comprising these catalyst components display a good polymerization activity.

[0014] Particular preference is given to catalysts of the present invention which have a pentamethylated cyclopentadienyl ring as ligand and 3 fluorine atoms on the metal atom M1. Catalyst systems comprising these catalyst components display a very good polymerization activity.

[0015] Particular preference is given to titanium as transition metal atom. Titanium as transition metal gives predominantly good polymerization activities.

[0016] The present invention provides a catalyst component comprising at least one bridge R9 between at least two radicals Ra. R9 is preferably 1

[0017] where R10 and R11 are identical or different and are each a hydrogen atom, a halogen atom or a C1-C40-group such as a C1-C20-alkyl group, a C1-C10-fluoroalkyl group, a C1-C10-alkoxy group, a C6-C14-aryl group, a C6-C10-fluoroaryl group, a C6-C10-aryloxy group, a C2-C10-alkenyl group, a C7-C40-arylalkyl group, a C7-C40-alkylaryl group or a C8-C40-arylalkenyl group or R10 and R11, in each case together with the atoms connecting them, form one or more rings, and x is an integer from zero to 18, M2 is silicon, germanium or tin. R9 can also link two units of the formula (I) to one another.

[0018] The following examples illustrate the organometallic fluorides described by the formula I, but make no claim to completeness:

[0019] ethylenebis(indenyl)zirconium difluoride

[0020] ethylenebis(4,5,6,7-tetrahydroindenyl)zirconium difluoride

[0021] ethylenebis(2-methylindenyl)zirconium difluoride

[0022] ethylenebis(2,4-dimethylindenyl)zirconium difluoride

[0023] dimethylsilanediylbis(2-methyl-4,5-benzoindenyl)zirconium difluoride

[0024] dimethylsilanediylbis(2-methyl-4,6-diisopropylindenyl)zirconium difluoride

[0025] dimethylsilanediylbis(2-methyl-4-phenylindenyl)zirconium difluoride

[0026] dimethylsilanediylbis(2-ethyl-4-phenylindenyl)zirconium difluoride

[0027] dimethylsilanediylbis(2-methyl-4-(1-naphthyl)indenyl)zirconium difluoride

[0028] dimethylsilanediylbis(indenyl)zirconium difluoride

[0029] dimethylsilanediylbis(2-methyl-4-ethylindenyl)zirconium difluoride

[0030] dimethylsilanediylbis(2-methyl-4-isopropylindenyl)zirconium difluoride

[0031] dimethylsilanediylbis(2-methyl-4-methylindenyl)zirconium difluoride

[0032] dimethylsilanediylbis(2-ethyl-4-methylindenyl)zirconium difluoride

[0033] dimethylsilanediylbis(2-methyl-α-acenaphth-1-indenyl)zirconium difluoride

[0034] phenylmethylsilanediylbis(2-methyl-4-phenylindenyl)zirconium difluoride

[0035] phenylmethylsilanediylbis(2-methylindenyl)zirconium difluoride

[0036] ethylenebis(2-methyl-4,5-benzoindenyl)zirconium difluoride

[0037] ethylenebis(2-methyl-4,6-diisopropylindenyl)zirconium difluoride

[0038] ethylenebis(2-methyl-4-phenylindenyl)zirconium difluoride

[0039] ethylenebis(2-ethyl-4-phenylindenyl)zirconium difluoride

[0040] ethylenebis(2-methyl-4-(1-naphthyl)indenyl)zirconium difluoride

[0041] ethylenebis(indenyl)zirconium difluoride

[0042] ethylenebis(2-methyl-4-ethylindenyl)zirconium difluoride

[0043] ethylenebis(2-methyl-4-isopropylindenyl)zirconium difluoride

[0044] ethylenebis(2-methyl-4-methylindenyl)zirconium difluoride

[0045] ethylenebis(2-ethyl-4-methylindenyl)zirconium difluoride

[0046] ethylenebis(2-methyl-α-acenaphth-1-indenyl)zirconium difluoride

[0047] bis(2-methyl-4,5-benzoindenyl)zirconium difluoride

[0048] bis(2-methyl-4,6-diisopropylindenyl)zirconium difluoride

[0049] bis(2-methyl-4-phenylindenyl)zirconium difluoride

[0050] bis(2-ethyl-4-phenylindenyl)zirconium difluoride

[0051] bis(2-methyl-4-(1-naphthyl)indenyl)zirconium difluoride

[0052] bis(indenyl)zirconium difluoride

[0053] bis(2-methyl-4-ethylindenyl)zirconium difluoride

[0054] bis(2-methyl-4-isopropylindenyl)zirconium difluoride

[0055] bis(2-methyl-4-methylindenyl)zirconium difluoride

[0056] bis(2-ethyl-4-methylindenyl)zirconium difluoride

[0057] bis(2-methyl-α-acenaphth-1-indenyl)zirconium difluoride

[0058] bis(n-butylcyclopentadienyl)zirconium difluoride

[0059] bis(cyclopentadienyl)zirconium difluoride

[0060] bis(pentamethylcyclopentadienyl)zirconium difluoride

[0061] cyclopentadienylzirconium trifluoride

[0062] pentamethylcyclopentadienylzirconium trifluoride

[0063] (2-methyl-4,5-benzoindenyl)zirconium trifluoride

[0064] (2-methyl-4,6-diisopropylindenyl)zirconium trifluoride

[0065] (2-methyl-4-phenylindenyl)zirconium trifluoride

[0066] (2-ethyl-4-phenylindenyl)zirconium trifluoride

[0067] (2-methyl-4-(1-naphthyl)indenyl)zirconium trifluoride

[0068] indenylzirconium trifluoride

[0069] (2-methyl-4-ethylindenyl)zirconium trifluoride

[0070] (2-methyl-4-isopropylindenyl)zirconium trifluoride

[0071] (2-methyl-4-methylindenyl)zirconium trifluoride

[0072] (2-ethyl-4-methylindenyl)zirconium trifluoride

[0073] (2-methyl-α-acenaphth-1-indenyl)zirconium trifluoride

[0074] (n-butylcyclopentadienyl)zirconium trifluoride

[0075] isopropylidene(9-fluorenyl)cyclopentadienylzirconium difluoride

[0076] diphenylmethylene(9-fluorenyl)cyclopentadienylzirconium difluoride

[0077] phenylmethylmethylene(9-fluorenyl)cyclopentadienylzirconium difluoride

[0078] dimethylsilanediyl(9-fluorenyl)cyclopentadienylzirconium difluoride

[0079] isopropylidene(9-fluorenyl)(3-methylcyclopentadienyl)zirconium difluoride

[0080] diphenylmethylene(9-fluorenyl)(3-methylcyclopentadienyl)zirconium difluoride

[0081] phenylmethylmethylene(9-fluorenyl)(3-methylcyclopentadienyl)zirconium difluoride

[0082] dimethylsilanediyl(9-fluorenyl)(3-methylcyclopentadienyl)zirconium difluoride

[0083] isopropylidene(9-fluorenyl)(3-isopropylcyclopentadienyl)zirconium difluoride

[0084] diphenylmethylene(9-fluorenyl)(3-isopropylcyclopentadienyl)zirconium difluoride

[0085] phenylmethylmethylene(9-fluorenyl)(3-isopropylcyclopentadienyl)zirconium difluoride

[0086] dimethylsilanediyl(9-fluorenyl)(3-isopropylcyclopentadienyl)zirconium difluoride

[0087] isopropylidene(2,7-ditert-butyl-9-fluorenyl)cyclopentadienylzirconium difluoride

[0088] diphenylmethylene(2,7-ditert-butyl-9-fluorenyl)cyclopentadienylzirconium difluoride

[0089] phenylmethylmethylene(2,7-ditert-butyl-9-fluorenyl)cyclopentadienylzirconium difluoride

[0090] dimethylsilanediyl(2,7-ditert-butyl-9-fluorenyl)cyclopentadienylzirconium difluoride

[0091] ethylenebis(indenyl)titanium difluoride

[0092] ethylenebis(4,5,6,7-tetrahydroindenyl)titanium difluoride

[0093] ethylenebis(2-methylindenyl)titanium difluoride

[0094] dimethylsilanediylbis(indenyl)titanium difluoride

[0095] bis(indenyl)titanium difluoride

[0096] bis(cyclopentadienyl)titanium difluoride

[0097] bis(pentamethylcyclopentadienyl)titanium difluoride

[0098] cyclopentadienyltitanium trifluoride

[0099] pentamethylcyclopentadienyltitanium trifluoride

[0100] indenyltitanium trifluoride

[0101] (n-butylcyclopentadienyl)titanium trifluoride

[0102] isopropylidene(9-fluorenyl)cyclopentadienyltitanium difluoride

[0103] ethylenebis(indenyl)hafnium difluoride

[0104] ethylenebis(4,5,6,7-tetrahydroindenyl)hafnium difluoride

[0105] ethylenebis(2-methylindenyl)hafnium difluoride

[0106] dimethylsilanediylbis(indenyl)hafnium difluoride

[0107] bis(indenyl)hafnium difluoride

[0108] bis(cyclopentadienyl)hafnium difluoride

[0109] bis(pentamethylcyclopentadienyl)hafnium difluoride

[0110] cyclopentadienylhafnium trifluoride

[0111] pentamethylcyclopentadienylhafnium trifluoride

[0112] indenylhafnium trifluoride

[0113] (n-butylcyclopentadienyl)hafnium trifluoride

[0114] isopropylidene(9-fluorenyl)cyclopentadienylhafnium difluoride

[0115] bis(cyclopentadienyltitanium)fluoride

[0116] bis(methylcyclopentadienyltitanium fluoride)

[0117] bis(pentamethylcyclopentadienyltitanium)fluoride

[0118] [(Me3SiC5H4)Ti(F)Nt—Bu]2

[0119] The organometallic halides required as starting compounds are commercially available or can be prepared by methods known from the literature. The tin fluorides required as starting materials can be prepared by methods known from the literature (Ber. Dtsch. Chem. Ges. (1918), vol. 51, 1447).

[0120] The present invention provides a catalyst system comprising at least one catalyst component and at least one organic boron compound and/or at least one organic aluminum compound and/or at least one organic tin compound as cocatalyst. The catalyst system is obtainable by bringing at least one catalyst component into contact with at least one organic boron compound and/or at least one organic aluminum compound and/or at least one organic tin compound. This forms, in particular, the reaction product of at least one catalyst component and at least one organic boron compound and/or organic aluminum compound and/or organic tin compound and also reaction products of these compounds with condensation agents such as water. Very good polymerization activities are obtained using these catalyst systems. The cocatalyst component which, according to the present invention, may be present in the catalyst system comprises at least one compound of the aluminoxane, Lewis acid or ionic type which is converted into a cationic compound by reaction with a catalyst component.

[0121] As aluminoxane, preferance is given to using a compound of the formula II

(R AlO)n  (II).

[0122] Aluminoxanes can be, for example, cyclic as in formula III 2

[0123] or linear as in formula IV 3

[0124] or of the cluster type as in formula V, as described in more recent literature; cf. JACS 117 (1995), 6465-74, Organometallics 13 (1994), 2957-2969. 4

[0125] The radicals R in the formulae (II), (III), (IV) and (V) can be identical or different and be a C1-C20-hydrocarbon group such as a C1-C6-alkyl group, a C6-C18-aryl group, benzyl or hydrogen, and p is an integer from 2 to 50, preferably from 10 to 35.

[0126] The organic radicals are preferably identical and are methyl, isobutyl, n-butyl, phenyl or benzyl, particularly preferably methyl. If the organic radicals are different, they are preferably methyl and hydrogen, methyl and isobutyl or methyl and n-butyl, with hydrogen, isobutyl or n-butyl being present. As Lewis acid, preference is given to using at least one organoboron or organoaluminum compound which contains C1-C20-groups such as branched or unbranched alkyl or haloalkyl groups.

[0127] The present invention provides a catalyst system which may further comprise a support. The support component of the catalysts system of the present invention is preferably at least one inorganic oxide such as SiO2, Al2O3, MgO, ZrO2, TiO2, B2O3, CaO, ZnO, ThO2, carbonates such as Na2CO3, K2CO3, CaCO3, MgCO3, sulfates such as Na2SO4, Al2(SO4)3, BaSO4, nitrates such as KNO3, Mg(NO3)2, Al(NO3)3 and also oxides such as Na2O, K2O and Li2O. Supports employed are, in particular, silica and/or alumina and/or polymer supports. The present invention provides polymers and/or copolymers obtainable by polymerization using a catalyst system according to the present invention. Polymers and/or copolymers of 1-alkenes and vinylaromatics obtainable by polymerization using a catalyst system according to the present invention are particularly preferred. Syndiotactic polymers obtainable by polymerization using a catalyst system according to the present invention are very particularly preferred. Syndiotactic polystyrene obtainable by polymerization using a catalyst system according to the present invention is most preferred.

[0128] To polymerize preferably vinylaromatic monomers by the method according to the present invention, fluorine-containing transition metal compounds as catalyst component, organic boron compounds and/or organic aluminum compounds and/or organic tin compounds and reaction products of these with condensation agents, e.g. water, as cocatalyst component and also vinylaromatic monomer are used in any order. It is possible to use one or more supports. One or more solvents can be added thereto in any order. The introduction of the components and the reaction are carried out at atmospheric pressure or under subatmospheric or superatmospheric pressure in an inert gas atmosphere, e.g. nitrogen, argon or a mixture thereof. The reaction is preferably carried out in the temperature range of from 10 to 70° C. The constituents of the catalyst system are used in any molar ratio to one another. Preference is given to a ratio of aluminum to titanium of 100:1000.

[0129] The invention provides for the use of a catalyst system for preparing a polymer and/or copolymer, particularly for the polymerization and/or copolymerization of 1-alkenes and vinylaromatics, very particularly for the polymerization of styrene.

[0130] The invention is illustrated by the examples.

EXAMPLES

Example 1

[0131] A 100 ml glass reactor heated to 50° C. was charged in a counter-current of argon while stirring with, in succession, 14.1 ml of toluene, 5 ml of a methylaluminoxane solution in toluene (7.5×10−4 mol/5 ml), 20 ml of styrene and 0.9 ml of a toluene solution of cyclopentadienyltitanium trifluoride (2.5×10−6 mol/0.9 ml). The addition of the titanium compound was taken as the starting point of the polymerization. After 10 minutes, about 50 ml of a mixture of hydrochloric acid and ethanol were added. Stirring was continued for a further 12 hours. The solid product was filtered off and washed with ethanol until neutral. The polymer was dried under reduced pressure at room temperature.

Comparative Example 1

[0132] Comparative Example 1 was carried out as described in Example 1, but using CpTiCl3 as catalyst.

Example 2

[0133] Example 2 was carried out as described in Example 1, but using Cp*TiF3 as catalyst.

Comparative Example 2

[0134] Comparative Example 2 was carried out as described in Example 1, but using Cp*TiCl3 as catalyst.

[0135] Table 1 below shows the polymerization activities of the catalysts used in Example 1 and Comparative Example 1 and the characteristic data of the polymers obtained in Example 1 and Comparative Example 1.

	TABLE 1
	Comparative Example 1	Example 1
	CpTiCl3a)	CpTiF3a)
T(°C.)b)	10	30	50	70	10	30	50	70
t(h)c)	0.22	0.08	0.12	0.25	0.52	0.14	0.17	0.43
[Ti]j)	6.25	6.25	6.25	6.25	6.25	6.25	6.25	6.25
	× 10−4	× 10−4	× 10−4	× 10−4	× 10−5	× 10−5	× 10−5	× 10−5
[Al]k)	1.88	1.88	1.88	1.88	1.88	1.88	1.88	1.88
	× 10−1	× 10−1	× 10−1	× 10−1	× 10−2	× 10−2	× 10−2	× 10−2
Yield	600	990	3390	2880	330	830	1270	1860
(mg)d)
Activ.e)	110	480	1200	460	250	2400	3100	1700
M.p. (°C.)f)	260/	263	258/	243/	264	261/	257/	247/
	267		250	250		267	265	258
MWg)	390	230	115	40	867	378	96	35
Mnh)	110	107	44	17	557	162	53	17
MW/Mni)	3.56	2.15	2.60	2.47	1.56	2.34	1.82	2.09

[0136] Table 2 below shows the polymerization activities of the catalysts used in Example 2 and Comparative Example 2 and the characteristic data of the polymers obtained in Example 2 and Comparative Example 2.

	TABLE 2
	Comparative Example 2	Example 2
	Cp*TiCl3a)	Cp*TiF3a)
T(°C.)b)	10	30	50	70	10	30	50	70
t(h)c)	2.80	1.03	1.00	0.77	0.52	0.35	0.22	0.23
[Ti]j)	6.25	6.25	6.25	6.25	6.25	6.25	6.25	6.25
	× 10−4	× 10−4	× 10−4	× 10−4	× 10−5	× 10−5	× 10−5	× 10−5
[Al]k)	1.88	1.88	1.88	1.88	1.88	1.88	1.88	1.88
	× 10−1	× 10−1	× 10−1	× 10−1	× 10−2	× 10−2	× 10−2	× 10−2
Yield	49	90	385	730	49	240	375	650
(mg)d)
Activ.e)	0.7	3.5	15.4	38	38	270	690	1100
M.p. (°C.)f)	276	277	275	274	274	275	275	275
MWg)	170	189	169	156	966	703	661	511
Mnh)	62	82	47	43	512	353	367	193
MW/Mni)	2.75	2.31	3.63	3.61	1.89	1.99	1.80	2.64

Example 3

[0137] A 200 ml glass reactor heated to 30° C. was charged in a countercurrent of argon while stirring with, in succession, 49 ml of toluene, 0.58 g (0.01 mol) of methylaluminoxane, 50 ml of styrene and 1 ml of a toluene solution of methylcyclopentadienyltitanium trifluoride (10−5 mol/ml). The addition of the titanium compound was taken as the starting point of the polymerization. After 4 minutes, about 50 ml of a mixture of hydrochloric acid and ethanol were added. Stirring was continued for a further 12 hours. The solid product was filtered off and washed with ethanol until neutral. The polymer was dried under reduced pressure at room temperature.

Comparative Example 3

[0138] Comparative Example 3 was carried out as described in Example 3, but using methylcyclopentadienyltitanium trichloride as catalyst.

[0139] Table 3 below shows the polymerization activities of the catalysts used in Example 3 and Comparative Example 3 and the characteristic data of the polymers obtained in Example 3 and Comparative Example 3.

	TABLE 3
	Comparative Example 3	Example 3
	MeCpTiCl3a)	MeCpTiF3a)
	T(° C.)b)	30	30
	t (min)c)	60	4
	[Ti]j)	5 × 10−5	5 × 10−5
	[Al]k)	0.05	0.05
	Yield	494	482
	(mg)d)
	Activ.e)	99	1160
	M.p.	257	256
	(° C.)f)
	MWg)	261	304
	Mnh)	125	134
	MW/Mni)	2.09	2.27

Example 4 and Comparative Example 4

[0140] Example 4 was carried out as described in Example 3, but using EtMe4CpTiF3 as catalyst. Comparative Example 4 was carried out as described in Example 3, but using EtMe4CpTiCl3 as catalyst.

[0141] Table 4 below shows the polymerization activities of the catalysts used in Example 4 and Comparative Example 4 and the characteristic data of the polymers obtained in Example 4 and Comparative Example 4.

	TABLE 4
	Comparative Example 4	Example 4
	EtMe4CpTiCl3a)	EtMe4CpTiF3a)
	T(° C.)b)	30	30
	t(min)c)	120	10
	[Ti]j)	5 × 10−5	5 × 10−5
	[Al]k)	0.05	0.05
	Yield	110	140
	(mg)d)
	Activ.e)	11	167
	M.p.	277	270
	(° C.)f)
	MWg)	193	768
	Mnh)	94	395
	MW/Mni)	2.06	1.94

Example 5 and Comparative Example 5

[0142] Example 5 was carried out as described in Example 3, but using PrMe4CpTiF3 as catalyst. Comparative Example 5 was carried out as described in Example 3, but using PrMe4CpTiCl3 as catalyst.

[0143] Table 5 below shows the polymerization activities of the catalysts used in Example 5 and Comparative Example 5 and the characteristic data of the polymers obtained in Example 5 and Comparative Example 5.

	TABLE 5
	Comparative Example 5	Example 5
	PrMe4CpTiCl3a)	PrMe4CpTiF3a)
	T(° C.)b)	30	30
	t (min)c)	120	10
	[Ti]j)	5 × 10−5	5 × 10−5
	[Al]k)	0.05	0.05
	Yield	103	140
	(mg)d)
	Activ.e)	10	167
	M.p.	275	271
	(° C.)f)
	MWg)	153	636
	Mnh)	75	304
	MW/Mni)	2.05	2.09

Example 6 and Comparative Example 6

[0144] Example 6 was carried out as described in Example 3, but using BuMe4CpTiF3 as catalyst. Comparative Example 6 was carried out as described in Example 3, but using BuMe4CpTiCl3 as catalyst.

[0145] Table 6 below shows the polymerization activities of the catalysts used in Example 6 and Comparative Example 6 and the characteristic data of the polymers obtained in Example 6 and Comparative Example 6.

	TABLE 6
	Comparative Example 6	Example 6
	BuMe4CpTiCl3a)	BuMe4CpTiF3a)
	T (° C.)b)	30	30
	t (min)c)	120
	[Ti]j)	5 × 10−5	5 × 10−5
	[Al]k)	0.05
	Yield	121
	(mg)d)
	Activ.e)	12	185
	M.p.	276	273
	(° C.)f)
	MWg)	201	683
	Mnh)	93	309
	MW/Mni)	2.16	2.21

Examples 7, 8 and 9

[0146] Examples 7, 8 and 9 were carried out as described in Example 3, but using Cp*2TiF, Cp*TiF2(OCOC6F5) and Cp*TiF2(OCOCF3) as catalysts.

[0147] Table 7 below shows the polymerization activities of the catalysts used in Examples 7, 8 and 9 and the characteristic data of the polymers obtained.

	TABLE 7
	Example 7	Example 8	Example 9
	Cp*2TiFa)	Cp*TiF2(OCOC6F5)a)	Cp*TiF2(OCOCF3)a)
T (° C.)b)	30	30	30
t (min)c)	60	8	10
[Ti]j)	5 × 10−5	10−4	10−4
[Al]k)	0.05	0.1	0.1
Yield	174	678	381
(mg)d)
Activ.e)	35	510	229
M.p. (° C.)f)	270	269	269
MWg)	612	543	558
Mnh)	250	249	261
MW/Mni)	2.45	2.18	2.14
a)Cp = cyclopentadienyl, Cp* = pentamethylcyclopentadienyl, Me = methyl, Et = ethyl, Pr = propyl and Bu = butyl
b)polymerization temperature
c)polymerization time
d)yield of syndiotactic polystyrene
e)polymerization activity of the catalyst system as yield of syndiotactic polystyrene (sPS) in kg based on the molar amount of titanium compound in mol and based on the polymerization time in h: (kg sPS/mol Ti × h)
f)melting point(s) of the polystyrene from the 2nd heating curve of the DSC (differential scanning calorimetry)
g)weight average molecular weight of the polystyrene divided by 1000, determined by GPC (gel permeation chromatography)
h)number average molecular weight of the polystyrene divided by 1000, determined by GPC (gel permeation chromatography)
i)polydispersity of the polystyrene, determined by GPC (gel permeation chromatography)
j)concentration of the titanium compound in mol/l
k)concentration of methylaluminoxane in mol/l

Claims

1. A catalyst component for the polymerization of olefins, comprising at least one compound of the formula (I):

2. A catalyst component as claimed in claim 1, comprising at least one bridge R9 between at least two radicals Ra, R9 is preferably

3. A catalyst system comprising at least one catalyst component and at least one organic boron compound and/or at least one organic aluminum compound and/or at least one organic tin compound.

4. A catalyst system as claimed in claim 3, obtainable by bringing at least one catalyst component into contact with at least one organic boron compound and/or at least one organic aluminum compound and/or at least one organic tin compound.

5. A catalyst system as claimed in claim 3 or 4, comprising at least one inorganic and/or organic support.

6. A polymer and/or copolymer obtainable by polymerization using a catalyst system as claimed in any of claims 3 to 5.

7. A polymer and/or copolymer of 1-alkenes and vinylaromatics, obtainable by polymerization using a catalyst system as claimed in any of claims 3 to 5.

8. A syndiotactic polymer obtainable by polymerization using a catalyst system as claimed in any of claims 3 to 5.

9. A syndiotactic polystyrene obtainable by polymerization using a catalyst system as claimed in any of claims 3 to 5.

10. A process for polymerization and/or copolymerization using a catalyst system as claimed in any of claims 3 to 5.

11. A process as claimed in claim 10 for polymerization and/or copolymerization of 1-alkenes and vinylaromatics.

12. A process as claimed in claim 10 or 11 for the polymerization of styrene to syndiotactic polystyrene.

13. The use of a catalyst system for preparing a polymer and/or copolymer, particularly for the polymerization and/or copolymerization of 1-alkenes and vinylaromatics, very particularly for the polymerization of styrene.