The novel metallocenes of the formula I ##STR1##

in which, preferably, M1 is Zr or Hf, r1 and r2 are alkyl or halogen, r3 and r4 are hydrogen, r5 and r6 are alkyl or haloalkyl, --(CR8 r9)m --r7 --(CR8 r9)n -- is a single- or multi-membered chain in which r7 may also be a (substituted) hetero atom, m+n is zero or 1, and r10 is hydrogen, form, together with aluminoxanes as cocatalysts, a very effective catalyst system for the preparation of polyolefins or high stereospecificity and high melting point. polyolefins with unique or improved properties are obtained by polymerizing an olefin in the presence of a metallocene combined with a cocatalyst, wherein the metallocene is preferably a zirconocene or a hafnocene, and the Zr or Hf central atom is coordinated with two ligands which are derivatives of 2-substituted indenyl nuclei and which are substituted with at least one and up to four groups (e.g. aliphatic or aromatic groups) on the six-member rings of the indenyl nuclei. The indenyl nuclei are optionally substituted at the 3-position and are joined by a 1,1'-bridge of the formula --(CR8 r9)m --r7 --(CR8 r9)n --, which is a single- or multi-membered chain in which r7 can also be a (substituted) hetero atom, m and n are identical or different and are zero, 1, or 2, and m+n is zero, 1, or 2.

Patent
   RE37208
Priority
Nov 12 1990
Filed
Oct 17 1994
Issued
Jun 05 2001
Expiry
Jun 05 2018
Assg.orig
Entity
Large
22
34
all paid

REINSTATED
1. A compound of the formula I for preparing essentially isotactic olefin polymers ##STR11##
in which
M1 is a metal from group ivb, Vb or VIb of the Periodic Table
r1 and r2 are identical or different and are a hydrogen atom, a C1 -C10 -alkyl group, a C1 -C10 -alkoxy group, a C6 -C10 -aryl group, a C6 -C10 -aryloxy group, a C2 -C10 -alkenyl group, a C7 -C40 -arylalkyl group, a C7 -C40 -alkylaryl group, a C8 -C40 -arylalkenyl group or a halogen atom,
r3 and r4 are identical or different and are a hydrogen atom, a halogen atom, a halogen atom, a C1 -C10 -alkyl group, which is optionally halogenated, a C6 -C10 -aryl group, an --NR215, --SR15, --OSiR315, --SiR315 or --PR215 radical in which r15 is a halogen atom, a C1 -C10 -alkyl group or a C6 -C10 -aryl group, r5 and r6 are identical or different and are as defined for r3 and r4, with the proviso that r5 and r6 are not hydrogen,
r7 is ##STR12##
where
r11, r12 and r13 are identical or different and are a hydrogen atom, a halogen atom, a C1 -C10 -alkyl group, a C1 -C10 -fluoroalkyl group, a C6 -C10 -aryl group, a C6 -C10 -fluoroaryl group, a C1 -C10 -alkoxy group, a C2 -C10 -alkenyl group, a C7 -C40 -arylalkyl group, a C8 -C40 -arylalkenyl group or a C7 -C40 -alkylaryl group, or r11 and r12 or r11 and r13, in each case with the atoms connecting them, form a ring,
M2 is silicon, germanium or tin,
r8 and r9 are identical or different and are as defined for r11
m and n are identical or different and are zero, 1 or 2, m plus n being zero, 1 or 2, and
the radicals r10 are identical or different and are as defined for r11, r12 and r13.
16. A polyolefin made by polymerizing an olefin in the presence of a combination comprising a metallocene compound and a cocatalyst, said metallocene compound being a compound of the formula I: ##STR14##
in which
M1 is a metal from group ivb, Vb or VIb of the Periodic Table
r1 and r2 are identical or different and are a hydrogen atom, a C1 -C10 -alkyl group, a C1 -C10 -alkoxy group, a C6 -C10 -aryl group, a C6 -C10 -aryloxy group, a C2 -C10 -alkenyl group, a C7 -C40 -arylalkyl group, a C7 -C40 -alkylaryl group, a C8 -C40 -arylalkenyl group or a halogen atom,
r3 and r4 are identical or different and are a hydrogen atom, a halogen atom, a C1 -C10 -alkyl group, which is optionally halogenated, a C6 -C10 -aryl group, an --NR215, --SR15, --OSiR315, --SiR315 or --PR215 radical in which r15 is a halogen atom, a C1 -C10 -alkyl group or a C6 -C10 -aryl group,
r5 and r6 are identical or different and are as defined for r3 and r4, with the proviso that r5 and r6 are not hydrogen, ##STR15##
where
r11, r12 and r13 are identical or different and are a hydrogen atom, a halogen atom, a C1 -C10 -alkyl group, a C1 -C10 -fluoroalkyl group, a C6 -C10 -aryl group, a C6 -C10 -fluoroaryl group, a C1 -C10 -alkoxy group, a C2 -C10 -alkenyl group, a C7 -C40 -arylalkyl group, a C8 -C40 -arylalkenyl group or a C7 -C40 -alkylaryl group, or a pair of substituents r11 and r12 or r11 and r13 in each case with the atoms connecting them, form a ring,
M2 is silicon, germanium or tin,
r8 and r9 are identical or different and are as defined for r11
m and n are identical or different and are zero, 1 or 2, m plus n being zero, 1 or 2, and
the radicals r10 are identical or different and are as defined for r11, r12 and r13, except that at least one of the r10 radicals is not hydrogen.
2. A compound of the formula I as claimed in claim 1, wherein, in the formula I, M1 is Zr or Hf, r1 and r2 are identical or different and are methyl or chlorine, r3 or r4 are hydrogen, r5 and r6 are identical or different and are methyl, ethyl or trifluoromethyl, r7 is a ##STR13##
n plus m is zero or 1, and r10 is hydrogen.
3. A compound of the formula I as claimed in claim 1 wherein the compound is rac-dimethylsilyl(2-methyl-4,5,6,7-tetrahydro-1-indenyl)2 zirconium dichloride, rac-ethylene(2-methyl4,5,6,7-tetrahydro-1-indenyl)2 zirconium dichloride, rac-dimethylsilyl (2-methyl-4,5,6,7-tetrahydro-1-indenyl)2 dimethylzirconium or rac-ethylene(2-methyl-4,5,6,7-tetrahydro-1-indenyl)2 dimethylzirconium.
4. A compound as claimed 1, wherein M1 is zirconium, hafnium or titanium.
5. A compound as claimed in claim 1, wherein r1 and r2 are identical or different and are a hydrogen atom, a C1 -C3 -alkyl group, a C1 -C3 -alkoxy group, a C6 -C8 -aryl group, a C6 -C8 -aryloxy group, a C2 -C4 -alkenyl group, a C7 -C10 -arylalkyl group, a C7 -C12 -alkylaryl group, a C8 -C12 -arylalkenyl group or chlorine.
6. A compound as claimed in claim 1, wherein r3 and r4 are identical or different and are a hydrogen atom, a fluorine, chlorine or bromine atom, a C1 -C4 -alkyl group which may be halogenated, a C6 -C8 -aryl group, a --NR215, --SR15, --OSiR315, --SiR315 or --PR215 radical in which r15 is a chlorine atom, or a C1 -C3 -alkyl group or a C6 -C8 -aryl group.
7. A compound as claimed in claim 1, wherein r3 and r4 are hydrogen.
8. A compound as claimed in claim 1, wherein r5 and r6 are identical.
9. A compound as claimed in claim 1, wherein r5 and r6 are (C1 -C4)-alkyl, which may be halogenated with methyl.
10. A compound as claimed in claim 1, wherein r11, r12 and r13 are identical or different and are a hydrogen atom, a halogen atom, a C1 -C4 -alkyl group, a CF3 group, a C6 -C8 -aryl group, a pentafluorophenyl group, a C1 -C4 -alkoxy group, a C2 -C4 -alkenyl group, a C7 -C10 -arylalkyl group, a C8 -C12 -arylalkenyl group or a C7 -C14 -alkylaryl group, or r11 and r12 or r11 and r13, in each case together with the atoms connecting them, form a ring.
11. A compound as claimed in claim 1, wherein M2 is silicon or germanium.
12. A compound as claimed in claim 1, wherein r7 is ═CR11 r12, ═SiR11 r12, ═GeR11 r12, --O--, --S--, ═SO, ═PR11 or ═P(O)r11.
13. A compound as claimed in claim 1, wherein m and n are identical or different and are zero or 1.
14. A compound as claimed in claim 1, wherein m plus n is zero or 1.
15. A compound as claimed in claim 1, wherein r10 is hydrogen or C1 -C4 -alkyl groups.
17. The polyolefin as claimed in claim 16, wherein said combination comprises said metallocene compound of formula I and an aluminoxane.

The present invention relates to novel metallocenes which contain ligands of 2-substituted indenyl derivatives and can very advantageously be used as catalysts in the preparation of polyolefins of high melting point (high isotacticity).

Polyolefins of relatively high melting point and thus relatively high crystallinity and relatively high hardness are particularly important as engineering materials (for example large hollow articles, tubes and moldings).

Chiral metallocenes are, in combination with aluminoxanes, active, stereospecific catalysts for the preparation of polyolefins (U.S. Pat. No. 4,769,510). These metallocenes also include substituted indene compounds. Thus, for example, the use of the ethylenebis(4,5,6,7-tetrahydro-1-indenyl)zirconium dichloride/aluminoxane catalyst system is known for the preparation of isotactic polypropylene; cf. EP-A 185 918). Both this and numerous other polymerization processes coming under the prior art have, in particular, the disadvantage that, at industrially interesting polymerization temperatures, only polymers of relatively low melting points are obtained. Their crystallinity and thus their hardness are too low for use as engineering materials.

Surprisingly, it has now been found that metallocenes which contain, as ligands, certain 2-substituted indenyl derivatives are suitable catalysts for the preparation of polyolefins of high isotacticity (melting point) and narrow molecular weight distribution.

The present invention therefore provides the compounds of the formula I below ##STR2##

in which

M1 is a metal from group IVb, Vb or VIb of the Periodic Table,

R1 and R2 are identical or different and are a hydrogen atom, a C1 -C10 -alkyl group, a C1 -C10 -alkoxy group, a C6 -C10 -aryl group, a C6 -C10 -aryloxy group, a C2 -C10 -alkenyl group, a C7 -C40 -arylalkyl group, a C7 -C40 -alkylaryl group, a C8 -C40 -arylalkenyl group or a halogen atom,

R3 and R4 are identical or different and are a hydrogen atom, a halogen atom, a C1 -C10 -alkyl group, which may be halogenated, a C6 -C10 -aryl group, an --NR215, --SR15, --OSiR315, --SiR315 or --PR215 radical in which R15 is a halogen atom, a C1 -C10 -alkyl group or a C6 -C10 -aryl group,

R5 and R6 are identical or different and are as defined for R3 and R4, with the proviso that R5 and R6 are not hydrogen,

R7 is ##STR3##

where

R11, R12 and R13 are identical or different and are a hydrogen atom, a halogen atom, a C1 -C10 -alkyl group, a C1 -C10 -fluoroalkyl group, a C6 -C10 -aryl group, a C6 -C10 -fluoroaryl group, a C1 -C10 -alkoxy group, a C2 -C10 -alkenyl group, a C7 -C40 -arylalkyl group, a C8 -C40 -arylalkenyl group or a C7 -C40 -alkylaryl group, or R11 and R12 or R11 and R13, in each case with the atoms connecting them, form a ring,

M2 is silicon, germanium or tin,

R8 and R9 are identical or different and are as defined for R11,

m and n are identical or different and are zero, 1 or 2, m plus n being zero, 1 or 2, and,

the radicals R10 are identical or different and are as defined for R11, R12 and R13.

Alkyl is straight-chain or branched alkyl. Halogen (halogenated) is fluorine, chlorine, bromine or iodine, preferably fluorine or chlorine.

In the formula I, M1 is a metal from group IVb, Vb or VIb of the Periodic Table, for example titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum or tungsten, preferably zirconium, hafnium or titanium.

R1 and R2 are identical or different and are a hydrogen atom, a C1 -C10 -, preferably C1 -C3 -alkyl group, a C1 -C10 -, preferably C1 -C3 -alkoxy group, a C6 -C10 -, preferably C6 -C8 -aryl group, a C6 -C10 -, preferably C6 -C8 -aryloxy group, a C2 -C10 -, preferably C2 -C4 -alkenyl group, a C7 -C40, preferably C7 -C10 -arylalkyl group, a C7 -C40 -, preferably C7 -C12 -alkylaryl group, a C8 -C40 -, preferably C8 -C12 -arylalkenyl group or a halogen atom, preferably chlorine.

R3 and R4 are identical or different and are a hydrogen atom, a halogen atom, preferably a fluorine, chlorine or bromine atom, a C1 -C10 -, preferably C1 -C4 -alkyl group, which may be halogenated, a C6 -C10 -, preferably C6 -C8 -aryl group, an --NR215, --SR15, --OSiR315, --SiR315 or --PR215 radical in which R15 is a halogen atom, preferably a chlorine atom, or a C1 -C10 -, preferably C1 -C3 -alkyl group or a C6 -C10 -, preferably C6 -C8 -aryl group. R3 and R4 are particularly preferably hydrogen.

R5 and R6 are identical or different, preferably identical, and are as defined for R3 and R4, with the proviso that R5 and R6 cannot be hydrogen. R5 and R6 are preferably (C1 -C4)-alkyl which may be halogenated, such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl or trifluoromethyl, in particular methyl.

R7 is ##STR4##

where R11, R12 and R13 are identical or different and are a hydrogen atom, a halogen atom, a C1 -C10 -, preferably C1 -C4 -alkyl group, in particular a methyl group, a C1 -C10 -fluoroalkyl group, preferably a CF3 group, a C6 -C10 -, preferably C6 -C8 -aryl group, a C6 -C10 -fluoroaryl group, preferably a pentafluorophenyl group, a C1 -C10 -, preferably C1 -C4 -alkoxy group, in particular a methoxy group, a C2 -C10 -, preferably C2 -C4 -alkenyl group, a C7 -C40 -, preferably C7 -C10 -arylalkyl group, a C8 -C40 -, preferably C8 -C12 -arylalkenyl group or a C7 -C40 -, preferably C7 -C12 -alkylaryl group, or R11 and R12 or R11 and R13, in each case together with the atoms connecting them, form a ring.

M2 is silicon, germanium or tin, preferably silicon or germanium.

R7 is preferably ═CR11 R12, ═SiR11 R12, ═GeR11 R12, --O--, --S--, ═SO, ═PR11 or ═P(O)R11.

R8 and R9 are identical or different and are as define as for R11.

m and n are identical or different and are zero, 1 or 2, preferably zero or 1, where m plus n is zero, 1 or 2, preferably zero or 1.

The radicals R10 are identical or different and are as defined for R11, R12 and R13. The radicals R10 are preferably hydrogen atoms or C1 -C10, preferably C1 -C4 -alkyl groups.

The particularly preferred metallocenes are thus those in which, in the formula I, M1 is Zr or Hf, R1 and R2 are identical or different and are methyl or chlorine, R3 and R4 are hydrogen, R5 and R6 are identical or different and are methyl, ethyl or trifluoromethyl, R7 is ##STR5##

radical, n plus m is zero or 1, and R10 is hydrogen; in particular the compounds I listed in the working examples.

Of the metallocenes I mentioned in the working examples, rac-dimethylsilyl(2-methyl-4,5,6,7-tetrahydro-1-indenyl)2 zirconium dichloride, rac-ethylene(2-methyl-4,5,6,7-tetrahydro-1-indenyl)2 zirconium dichloride, racdimethylsilyl(2-methyl-4,5,6,7-tetrahydro-1-indenyl)2 dimethylzirconium and rac-ethylene(2-methyl-4,5,6,7-tetrahydro-1-indenyl)2 dimethylzirconium are particularly important.

The chiral metallocenes are employed as racemates for the preparation of highly isotactic poly-1-olefins. However, it is also possible to use the pure R- or S-form. These pure stereoisomeric forms allow the preparation of an optically active polymer. However, the meso form of the metallocenes should be separated off since the polymerization-active center (the metal atom) in these compounds is no longer chiral due to mirror symmetry at the central metal, and it is therefore not possible to produce a highly isotactic polymer.

The principle of resolution of the stereoisomers is known.

The present invention furthermore provides a process for the preparation of the metallocenes I, which comprises

a) reacting a compound of the formula II ##STR6##

in which R3 -R10, m and n are defined in the formula I and M3 is an alkali metal, preferably lithium, with a compound of the formula III

M1 X4 (III)

in which M3 is a defined in the formula I, and X is a halogen atom, preferably chlorine, and catalytically hydrogenating the reaction product, or

b) reacting a compound of the formula IIa ##STR7##

with a compound of the formula III

M1 X4 (III)

in which all the substituents are as defined under a), and, if desired, derivatizing the reaction product obtained under a) or b).

The synthesis is carried out under a protective gas and in anhydrous solvents. The dried salt of the formula III/IIa is added to a suspension of the compound of the formula III in a solvent such as toluene, n-hexane, di-chloromethane, ether, THF, n-pentane or benzene, preferably dichloromethane or toluene. The reaction temperature is from -78° C. to 30°C, preferably from -40°C to 10°C The reaction duration is from 0.25 to 24 hours, preferably from 1 to 4 hours.

A further embodiment of the process according to the invention comprises replacing the compound III, M1 X4, by a compound of the formula IIIa, M1 X4 L2. In this formula, L is a donor ligand. Examples of suitable donor ligands are tetrahydrofuran, diethyl ether, dimethyl ether, inter alia, preferably tetrahydrofuran (THF).

In this case, a solution of the salt of the formula II/IIa in one of the abovementioned solvents is added to a solution or suspension of a compound of the formula IIIa in a solvent such as toluene, xylene, ether or THF, preferably THF. However, an alternative procedure is to simultaneously add both components dropwise to a solvent. This is the preferred procedure. The reaction temperature is from -40°C to 100°C, preferably from 0°C to 50°C, in particular from 10°C to 35°C The reaction duration is from 0.25 hour to 48 hours, preferably from 1 hour to 24 hours, in particular from 2 hours to 9 hours.

The hydrogenation is carried out in a dry, anhydrous solvent such as H2 CCl2 or glyme. The reaction temperature is 20° to 70°C, preferably from ambient temperature to 50°C, the pressure is from 5 to 200 bar, preferably from 20 to 120 bar, in particular from 35 to 100 bar, and the reaction duration is from 0.25 to 24 hours, preferably from 0.5 to 18 hours, in particular from 1 to 12 hours. Hydrogenation reactors which can be used are steel autoclaves. The hydrogenation catalyst used is platinum, platinum oxide, palladium or another conventional transition-metal catalyst.

The halogen derivatives obtained in this way can be converted into the alkyl, aryl or alkenyl complexes by known standard methods.

The compounds of the formulae II and IIa are synthesized by deprotonation. This reaction is known; cf. J. Am. Chem. Soc., 112 (1990) 2030-2031, ibid. 110 (1988) 6255-6256, ibid. 109 (1987), 6544-6545, J. Organomet. Chem., 322 (1987) 6570, New. J. Chem. 14 (1990) 499-503 and the working examples.

The synthesis of the protonated forms of the compounds of these formulae has also been described, with the difference that they are not correspondingly substituted in the α- and β-positions (Bull. Soc. Chim., 1967, 2954). The bridging units required for their synthesis are generally commercially available, but the indenyl compounds required, by contrast, are not. Some literature references containing synthesis procedures are indicated; the procedure for indene derivatives which are not mentioned is analogous: J. Org. Chem., 49 (1984) 4226-4237, J. Chem. Soc., Perkin II, 1981, 403-408, J. Am. Chem. Soc., 106 (1984) 6702, J. Am. Chem. Soc., 65 (1943) 567, J. Med. Chem., 30 (1987) 1303-1308, Chem. Ber. 85 (1952) 78-85 and the working examples.

The metallocenes I can thus in principle be prepared in accordance with the reaction scheme below: ##STR8##

The cocatalyst used according to the invention in the polymerization of olefins is an aluminoxane of the formula (IV) ##STR9##

for the linear type and/or of the formula (V) ##STR10##

for the cyclic type, where, in the formulae (IV) and (V), the radicals R may be identical or different and are a C1 -C6 -alkyl group, a C6 -C18 -aryl group or hydrogen, and p is an integer from 2 to 50, preferably from 10 to 35.

The radicals R are preferably identical and are methyl, isobutyl, phenyl or benzyl, particularly preferably methyl.

If the radicals R are different, they are preferably methyl and hydrogen or alternatively methyl and isobutyl, preferably from 0.01 to 40% (of the number of radicals R) being hydrogen or isobutyl.

The aluminoxane can be prepared in different ways by known processes. One of the methods is, for example, the reaction of an aluminum-hydrocarbon compound and/or a hydridoaluminum-hydrocarbon compound with water (gaseous, solid, liquid or bound--for example as water of crystallization) in an inert solvent (such as, for example, toluene). In order to prepare an aluminoxane containing different alkyl groups R, two different trialkylaluminum compounds (AlR3 +AlR'3) in accordance with the desired composition are reacted with water (cf. S. Pasynkiewicz, Polyhedron 9 (1990) 429 and EP-A 302 424).

The precise structure of the aluminoxanes IV and V is not known.

Irrespective of the preparation method, a varying content of unreacted aluminum starting compound, in free form or as an adduct, is common to all the aluminoxane solutions.

It is possible to preactivate the metallocene I using an aluminoxane of the formula (IV) and/or (V) before use in the polymerization reaction. This considerably increases the polymerization activity and improves the particle morphology.

The preactivation of the transition-metal compound is carried out in solution. The metallocene is preferably dissolved in a solution of the aluminoxane in an inert hydrocarbon. Suitable inert hydrocarbons are aliphatic or aromatic hydrocarbons. Toluene is preferred.

The concentration of the aluminoxane in the solution is in the range from about 1% by weight up to the saturation limit, preferably from 5 to 30% by weight, in each case based on the entire solution. The metallocene can be employed in the same concentration, but is preferably employed in an amount of from 10-4 -1 mol per mole of aluminoxane. The preactivation time is from 5 minutes to 60 hours, preferably from 5 to 60 minutes. The preactivation temperature is from -78°C to 100°C, preferably from 0 to 70°C

The metallocene can also be prepolymerized or applied to a support. The prepolymerization is preferably carried out using the olefin (or one of the olefin) employed in the polymerization.

Examples of suitable supports are silica gels, aluminum oxides, solid aluminoxane or other inorganic support materials. Another suitable support material is a polyolefin powder in finely divided form.

A further possible variation of the process comprises using a salt-like compound of the formula Rx NH4-x BR'4 or of the formula R3 PHBR'4 as cocatalyst instead of or in addition to an aluminoxane. x here is 1, 2 or 3, the R radicals are identical or different and are alkyl or aryl, and R' is aryl, which may also be fluorinated or partially fluorinated. In this case, the catalyst comprises the product of the reaction of a metallocene with one of said compounds (cf. EP-A 277 004).

The polymerization or copolymerization is carried out in a known manner in solution, in suspension or in the gas phase, continuously or batchwise, in one or more steps, at a temperature of from 0° to 150°C, preferably from 30° to 80°C Olefins of the formula Ra --CH═CH--Rb are polymerized or copolymerized. In this formula, Ra and Rb are identical or different and are a hydrogen atom or an alkyl radical having 1 to 14 carbon atoms.

However, Ra and Rb, together with the carbon atoms connecting them, may also form a ring. Examples of such olefins are ethylene, propylene, 1-butene, 1-hexene, 4-methyl-1-pentene, 1-octene, norbornene or norbornadiene. In particular, propylene and ethylene are polymerized.

The molecular weight regulator added, if necessary, is hydrogen. The overall pressure in the polymerization system is from 0.5 to 100 bar. The polymerization is preferably carried out in the industrially particularly interesting pressure range of from 5 to 64 bar.

The metallocene is used in a concentration, based on the transition metal, of from 10-3 to 10-8, preferably from 10-4 to 10-7 mol of transition metal per dm3 of solvent or per dm3 of reactor volume. The aluminoxane is used in a concentration of from 10-5 to 10-1 mol, preferably from 10-4 to 102 mol, per dm3 of solvent or per dm3 of reactor volume. In principle, however, higher concentrations are also possible.

If the polymerization is carried out as a suspension or solution polymerization, an inert solvent which is customary for the Ziegler low-pressure process is used. For example, the polymerization is carried out in an aliphatic or cycloaliphatic hydrocarbon; examples of these which may be mentioned are butane, pentane, hexane, heptane, isooctane, cyclohexane and methylcyclohexane.

It is also possible to use a petroleum ether or hydrogenated diesel oil fraction. Toluene can also be used.

The polymerization is preferably carried out in the liquid monomer.

If inert solvents are used, the monomers are metered in in gaseous or liquid form.

The polymerization can have any desired duration since the catalyst system to be used according to the invention exhibits only a low time-dependent drop in polymerization activity.

The process is distinguished by the fact that the metallocenes according to the invention give, in the industrially interesting temperature range of between 30° and 80°C, polymers of high molecular weight, high stereospecificity, narrow molecular weight dispersity and, in particular, high melting point, which is to say high crystallinity and high hardness.

The examples below are intended to illustrate the invention in greater detail.

The following abbreviations are used:

TBL VN = viscosity number in cm3 /g Mw = weight average molecular weight determined by gel Mw /Mn = molecular weight dispersity permeation chro- matography II = isotactic index (II = mm + 1/2 mr), determined by 13 C-NMR spectroscopy niso = length of the isotactic blocks (in propylen units) (niso = 1 + 2 mm/mr), determined by 13 C-NMR spectroscopy

The melting points and heats of melting Δ Hmelt were determined using DSC (heating and cooling rate 20°C/min).

Synthesis of the starting substances

I) Synthesis of 2-Me-indene

110.45 g (0.836 mol) of 2-indanone were dissolved in 500 ml of diethyl ether, and 290 cm3 of 3N (0.87 mol) ethereal methylGrignard solution were added dropwise at such a rate that the mixture refluxed gently. After the mixture had boiled for 2 hours under gentle reflux, it was transferred onto an ice/hydrochloric acid mixture, and a pH of 2-3 was established using ammonium chloride. The organic phase was separated off, washed with NaHCO3 and sodium chloride solution and dried, giving 98 g of crude product (2-hydroxy-2-methylindane), which was not purified further.

This product was dissolved in 500 cm3 of toluene, 3 g of p-toluenesulfonic acid were added, and the mixture was heated on a water separator until the elimination of water was complete, and was evaporated, the residue was taken up in dichloromethane, the dichloromethane solution was filtered through silica gel, and the filtrate was distilled in vacuo (80°C/10 mbar).

Yield: 28.49 g (0.22 mol/26%).

The synthesis of this compound is also described in: C. F. Koelsch, P. R. Johnson, J. Am. Chem. Soc., 65 (1943) 567-573.

II) Synthesis of (2-Me-indene)2 SiMe2

13 g (100 mmol) of 2-Me-indene were dissolved in 400 cm3 of diethyl ether, and 62.5 cm3 of 1.6N (100 mmol) n-butyllithium/n-hexane solution were added dropwise over the course of 1 hour with ice cooling, and the mixture was then stirred at ∼35°C for a further 1 hour.

6.1 cm3 (50 mmol) of dimethyldichlorosilane were introduced into 50 cm3 of Et2 O, and the lithio salt solution was added dropwise at 0°C over the course of 5 hours, the mixture was stirred overnight at room temperature and left to stand over the weekend.

The solid which had deposited was filtered off, and the filtrate was evaporated to dryness. The product was extracted using small portions of n-hexane, and the extracts were filtered and evaporated, giving 5.7 g (18.00 mmol) of white crystals. The mother liquor was evaporated, and the residue was then purified by column chromatography (n-hexane/H2 CCl2 9:1 by volume), giving a further 2.5 g (7.9 mmol/52%) of product (as an isomer mixture).

Rf (SiO2 ; n-hexane/H2 CCl2 9:1 by volume)=0.37.

The 1 H-NMR spectrum exhibits the signals expected for an isomer mixture with respect to shift and integration ratio.

III) Synthesis of (2-Me-Ind)2 CH2 CH2

3 g (23 mmol) of 2-Me-indene were dissolved in 50 cm3 of THF, 14.4 cm3 of 1.6N (23.04 mmol) n-butyllithium/n-hexane solution were added dropwise, and the mixture was then stirred at 65°C for 1 hour. 1 cm3 (11.5 mmol) of 1,2-dibromoethane was then added at -78° C., and the mixture was allowed to warm to room temperature and was stirred for 5 hours. The mixture was evaporated, and the residue was purified by column chromatography (SiO2 ; n-hexane/H2 CCl2 9:1 by volume).

The fractions containing the product were combined and evaporated, the residue was taken up in dry ether, the solution was dried over MgSO4 and filtered, and the solvent was stripped off.

Yield: 1.6 g (5.59 mmol/49%) of isomer mixture Rf (SiO2 ; n-hexane/H2 CCl2 9:1 by volume)=0.46.

The 1 H-NMR spectrum corresponds to expectations for an isomer mixture in signal shift and integration.

Synthesis of the metallocenes I

IV) rac-Dimethysilyl(2-Me-4,5,6,7-tetrahydro-1-indenyl)2 zirconium dichloride

a. Synthesis of the precursor rac-dimethylsilyl(2-Me-1-indenyl)2 zirconium dichloride

1.68 g (5.31 mmol) of the chelate ligand dimethylsilyl(2-methylindene)2 were introduced into 50 cm3 of THF, and 6.63 cm3 of a 1.6N (10.61 mmol) n-BuLi/n-hexane solution were added dropwise at ambient temperature over the course of 0.5 hour. The mixture was stirred for 2 hours at about 35°C, the solvent was stripped off in vacuo, and the residue was stirred with n-pentane, filtered off and dried.

The dilithio salt obtained in this way was added at -78°C to a suspension of 1.24 g (5.32 mmol) of ZrCl in 50 cm3 of CH2 Cl2, and the mixture was stirred at this temperature for 3 hours. The mixture was then warmed to room temperature overnight and evaporated. The 1 H-NMR spectrum showed, in addition to the presence of some ZrCl4 (thf)2, a rac/meso mixture. After stirring with n-pentane and drying, the solid, yellow residue was suspended in THF, filtered off and examined by NMR spectroscopy. These three working steps were repeated a number of times; finally, 0.35 g (0.73 mmol/14%) of product was obtained in which the rac form, according to 1 H-NMR, was enriched to more than 17:1.

The compound exhibited a correct elemental analysis and the following NMR signals (CDCl3, 100 MHz): δ=1.25 (s, 6H, Si-Me); 2.18 (s, 6H, 2-Me), 6.8 (s, 2H, 3-H-Ind); 6.92-7.75 (m, 8H, 4-7-H-Ind).

b. Synthesis of the end product

0.56 g (1.17 mmol) of the precursor rac-dimethylsilyl(2-Me-1-indenyl)2 zirconium dichloride were dissolved in 70 cm3 of CH2 Cl2 and the solution was introduced, together with 40 mg of PtO2, into a 200 cm3 NOVA stirred autoclave. The mixture was then stirred at room temperature for 4 hours under an H2 pressure of 40 bar. The filtrate was evaporated, the residue was washed with toluene/n-hexane (1:2 by volume), filtered and evaporated. N-pentane was added, and the suspension obtained was filtered off and dried. The yield was 0.34 g (0.7 mmol/60%). The 1 H-NMR spectrum (CD2 Cl2, 100 MHz) showed the following signals:

δ=0.90 (s, 6H, Me-Si); 1.43-1.93 (m, 8H, indenyl-H); 2.10 (s, 6H, 2-Me); 2.44-3.37 (m, 8H, indenyl-H); 6.05 (s, 2H, 3-H-Ind).

V) Synthesis of rac-ethylene(2-Me-4,5,6,7-tetrahydrol-indenyl)2 zirconium dichloride

a. Synthesis of the precursor rac-ethylene(2-Me-1-indenyl)2 zirconium dichloride

14.2 cm3 of 2.5N (35.4 mmol) n-BuLi/n-hexane solution were added dropwise over the course of 1 hour at room temperature to 5.07 g (17.7 mmol) of the ligand ethylene(2-methylindene)2 in 200 cm3 of THF, and the mixture was then stirred at about 50°C for 3 hours. A precipitate which formed temporarily dissolved again. The mixture was left to stand overnight.

6.68 g (17.7 mmol) of ZrCl4 thf)2 in 250 cm3 of THF were added dropwise, simultaneously with the above dilithio salt solution, to about 50 cm3 of THF at 50°C, and the mixture was then stirred at this temperature for 20 hours. The toluene extract of the evaporation residue was evaporated. The residue was extracted with a little THF, and the product was recrystallized from toluene, giving 0.44 g (0.99 mmol/5.6%) of product in which the rac form was enriched to more than 15:1.

The compound exhibited a correct elemental analysis and the following NMR signals (CDCl3, 100 MHz): δ=2.08 (2s, 6H, 2-Me); 3.45-4.18 (m, 4H, --CH2 CH2 --); 6.65 (2H, 3-H-Ind); 7.05-7.85 (m, 8H, 4-7-H-Ind).

b. Synthesis of the end product

56 g (1.25 mmol) of rac-ethylene(2-Me-1-indenyl)2 zirconium dichloride was dissolved in 50 cm3 of CH2 Cl2, and the solution was introduced, together with 40 mg of PtO2, into a 200 cm3 NOVA stirred autoclave. The mixture was then stirred at room temperature for 2 hours under an H2 pressure of 40 bar and evaporated to dryness, and the residue was sublimed in a high vacuum at a bath temperature of about 100°C, giving 0.46 g (1.01 mmol/81%) of product. The elemental analysis was correct, and the 1 H-NMR spectrum showed the following signals: δ=1.46-1.92 (m, 8H, indenyl-H), 2.14 (s, 6H, 2-Me); 2.49-2.73 (m, 6H, indenyl-H and --CH2 CH2 --), 2.89-3.49 (m, 6H, indenyl-H); 6.06 (s, 2H, 3-H-Ind).

VI) Me2 Zr[(2-Me-4,5,6,7-H4 -Ind)2 CH2 CH2 ]

5 cm3 of 1.6N (8 mmol) of ethereal methyllithium solution were added dropwise at -50°C to 1.27 g (2.79 mmol) of Cl2 Zr[(2-Me-4,5,6,7-H4 -Ind)2 CH2 CH2 ] in 20 cm3 of Et2 O, and the mixture was then stirred for 1 hour at -10°C The solvent was replaced by n-hexane, and the mixture was stirred for a further 2 hours at room temperature, filtered and evaporated.

Yield: 1 g (2.40 mmol/86%); correct elemental analysis.

VII) Me2 Zr[(2-Me-4,5,6,7-H4 -Ind)2 SiMe2 ]

4.3 cm3 of 1.6N (6.88 mmol) of ethereal methyllithium solution were added dropwise over the course of 15 minutes at -35°C to 1.33 g (2.74 mmol) of Cl2 Zr[(2-Me-4,5,6,7-H4 -Ind)2 SiMe2 ] in 25 cm3 of Et2 O. The mixture was stirred for 1 hour, the solvent was replaced by n-hexane, the mixture was stirred for 2 hours at 10°C and then filtered, the filtrate was evaporated, and the residue was sublimed in a high vacuum.

Yield: 1.02 g (2.49 mmol/89%); correct elemental analysis

VIII) Cl2 Zr[(2-Me-4,5,6,7-H4 -Ind)2 SiMePh]

1.5 g (2.78 mmol) of Cl2 Zr[(2-Me-Ind)2 SiMePh] and 60 mg of PtO2 in 80 cm3 of H2 CCl2 were hydrogenated for 5 hours at 40°C in a stirred autoclave under an H2 pressure of 30 bar. The mixture was filtered, the solvent was stripped off, and the residue was sublimed in a high vacuum.

Yield: 0.71 g (1.30 mmol/47%); correct elemental analysis

IX) Cl2 Zr[(2-Me-4,5,6,7-H4 -Ind)2 SiPh2 ]

0.8 g (1.33 mmol) of Cl2 Zr[(2-Me-Ind)2 SiPh2 ], dissolved in 50 cm3 of H2 CCl2, were stirred for 3 hours at 40°C with 30 mg of Pt under an H2 pressure of 50 bar. The mixture was filtered, the filtrate was evaporated, the residue was washed with warm n-hexane, the mixture was filtered, and the filtrate was evaporated.

Yield: 0.36 g (0.59 mmol/44%); correct elemental analysis

X) Cl2 Zr[(2-Et-4,5,6,7-H-Ind)2 CH2 CH2 ]

1.09 g (2.30 mmol) of Cl2 Zr[(2-Et-Ind)2 CH2 CH2 ] in 80 cm3 of H2 CCl2 were hydrogenated for 1 hour at ambient temperature together with 50 mg of PtO2 under an H2 pressure of 80 bar. The mixture was filtered, the filtrate was evaporated, and the residue was sublimed in a high vacuum.

Yield: 0.94 g (1.95 mmol/85%); correct elemental analysis

XI) Cl2 Zr[(2-Et-4,5,6,7-H4 -Ind)2 SiMe2 ]

2.00 g (3.96 mmol) of Cl2 Zr[(2-Et-Ind)2 SiMe2 ] in 100 cm3 of H2 CCl2 were hydrogenated for 3 hours at 35° C. together with 60 mg of PtO2 under an H2 pressure of 50 bar. The mixture was filtered, the filtrate was evaporated, and the residue was recrystallized from n-pentane.

Yield: 1.41 g (2.75 mmol/69%); correct elemental analysis

XII) Cl2 Zr[(2-Me-4,5,6,7-H4 -Ind)2 CHMeCH2 ]

0.80 g (1.73 mmol) of Cl2 Zr[(2-Me-Ind)2 CHMeCH2 ] in 40 cm3 of H2 CCl2 were stirred for 1 hour at ambient temperature together with 30 mg of PtO2 under an H2 pressure of 80 bar, the mixture was then filtered, the filtrate was evaporated, and the residue was sublimed.

Yield: 0.55 g (1.17 mmol/68%); correct elemental analysis

XIII) Cl2 Zr[(2-Me-4,5,6,7-H4 -Ind)2 CMe2 ]

0.3 g (0.65 mmol) of Cl2 Zr[(2-Me-Ind)2 CMe2 ] in 30 cm3 of H2 CCl2 were hydrogenated for 1 hour at ambient temperature together with 30 mg of Pt under an H2 pressure of 70 bar. The solvent was stripped off, and the residue was sublimed in a high vacuum.

Yield: 0.21 g (0.45 mmol/69%); correct elemental analysis

Abbreviations:

Me=methyl, Et=ethyl, Bu=butyl, Ph=phenyl,

Ind=indenyl, THF=tetrahydrofuran, PP=polypropylene,

PE=polyethylene.

Metallocenes I as catalysts for the polymerization of olefins

12 dm3 of liquid propylene were introduced into a dry 24 dm3 reactor which had been flushed with nitrogen. 35 cm3 of a toluene solution of methylaluminoxane (corresponding to 52 mmol of Al, mean degree of oligomerization n=17) were then added, and the batch was stirred at 30°C for 15 minutes. In parallel, 5.3 mg (0.011 mmol) of rac-dimethylsilyl(2-Me-4,5,6,7-tetrahydro-1-indenyl)2 zirconium dichloride were dissolved in 13.5 cm3 of a toluene solution of methylaluminoxane (20 mmol of Al) and preactivated by standing for 15 minutes. The solution was then introduced into the reactor and the polymerization system was heated to 70°C (over the course of 5 minutes) and kept at this temperature for 3 hours by cooling.

The activity of the metallocene was 50.3 kg of PP/g of metallocene×h.

VN=37 cm3 /g Mw =24 300 g/mol; Mw Mn =2.4; II=96.0%; niso =62; M.p.=150°C; ΔHmelt =104 J/g.

Example 1 was repeated, but 19.5 mg (0.04 mmol) of the metallocene were employed, and the polymerizaton temperature was 50°C

The activity of the metallocene was 18.8 kg of PP/g of metallocene×h.

VN=72 cm3 /g; M2 =64 750 g/mol; Mw /Mn=2.1; II=96.0%; niso =64; M.p.=154° C; ΔHmelt =109.5 J/g.

Example 1 was repeated, but 58.0 mg (0.12 mmol) of the metallocene were used and the polymerization temperature was 30°C

The activity of the metallocene was 9.7 kg of PP/g of metallocene×h.

VN=152 cm3 /g; Mw =171 000 g/mol; Mw /Mn =2.2; II=99.9%; niso =>500; M.p.=160°C; ΔHmelt =103 J/g.

Examples 1 to 3 were repeated, but the metallocenes dimethylsilyl(2-Me-1-indenyl)2 zirconium dichloride (metallocene 1), dimethylsilyl(4,5,6,7-tetrahydro-1-indenyl)2 zirconium dichloride (metallocene 2) and dimethylsilyl(1-indenyl)2 zirconium dichloride (metallocene 3) were used.

TBL Comp. Polym. M.p. ΔHmelt Ex. Metallocene temp. [°C] niso [°C] [J/g] A 1 70 38 145 86.6 B 1 50 48 148 88.1 C 1 30 48 152 90.2 D 2 70 34 141 -- E 2 50 38 143 -- F 3 70 32 140 -- G 3 50 34 142 -- H 3 30 37 145 --

Comparison of Comparative Examples F/G with D/E confirms the positive effect of the 4,5,6,7-tetrahydroindenyl ligand compared with indenyl, and Comparative Examples F/G/H compared with A/B/C show the positive effect of the substitution in the 2-position of the indenyl ligand.

In comparison with Examples 1 to 3, however, only the combination of substitution in the 2-position together with the tetrahydroindenyl system results in very high melting points and heats of melting and thus in high crystallinity and hardness of the polymers.

Example 1 was repeated, but 6.8 mg (0.015 mmol) of ethylene(2-Me-4,5,6,7-tetrahydro-1-indenyl)2 zirconium dichloride were employed.

The metallocene activity was 72.5 kg of PP/g of metallocene×h.

VN=35 cm3 /g; Mw =20 750 g/mol; Mw /Mn =1.9; II=94.5%; niso =34; M.p.=141°C; ΔHmelt =92.4 J/g.

Example 4 was repeated, but 28.1 mg (0.062 mmol) of the metallocene were used and the polymerization temperature was 50°C

The metallocene activity was 28.5 kg of PP/g of metallocene×h.

VN=51 cm3 /g; Mw =28 200 g/mol; Mw /Mn =2.2; II=94.8%; niso =35; M.p.=143°C; ΔHmelt =97.9 J/g.

Example 4 was repeated, but 50 mg (0.110 mmol) of the metallocene were used and the polymerization temperature was 30°C

The metallocene activity was 10.9 kg of PP/g of metallocene×h.

VN=92 cm3 /g; Mw =93 800 g/mol; Mw /Mn =2.2; II=95.5%; niso =48; M.p.=151°C; ΔHmelt =99.0 J/g.

Examples 4 to 6 were repeated, but the metallocenes ethylene(1-indenyl)2 zirconium dichloride (metallocene 4) and ethylene(2-Me-1-indenyl)2 zirconium dichloride (metallocene 5) were used.

TBL Comp. Polym. M.p. ΔHmelt Ex. Metallocene temp. [°C] niso [°C] [J/g] I 4 70 23 132 64.9 K 4 50 30 138 78.1 L 4 30 29 137 78.6 M 5 70 25 134 77.0 N 5 50 30 13S 7S.9 O 5 30 32 138 7S.6

Comparison of Comparative Examples I to O with Examples 4 to 6 confirms the effect of the substitution in the 2-position together with the use of the tetrahydroindenyl system. niso, melting point and heat of melting are significantly higher in each of Examples 4-6, and the crystallinity and hardness of the polymers are thus also significantly improved.

Winter, Andreas, Dolle, Volker, Spaleck, Walter, Antberg, Martin, Rohrmann, Jurgen

Patent Priority Assignee Title
10322224, Feb 10 2000 Baxter International Inc. Apparatus and method for monitoring and controlling a peritoneal dialysis therapy
11179516, Jun 22 2017 Baxter International Inc.; BAXTER HEALTHCARE SA Systems and methods for incorporating patient pressure into medical fluid delivery
6372848, Oct 10 2000 Baxter International Inc Blend of ethylene and α-olefin copolymers obtained using a metallocene catalyst for fabricating medical films and tubings
6420580, Nov 05 1999 Univation Technologies, LLC Catalyst compositions and method of polymerization therewith
6613713, Jan 28 2000 Bayer Aktiengesellschaft Organometallic compounds with fused indenyl ligands
6723676, Jun 08 2001 Bayer Aktiengesellschaft 1,3-disubstituted indene complexes
6964798, Nov 16 1993 Baxter International Inc Multi-layered polymer based thin film structure for medical grade products
7176158, Oct 25 2002 ExxonMobil Chemical Patents INC Polymerization catalyst composition
7238164, Jul 19 2002 BAXTER INTERNATIONAL, INC ; BAXTER HEALTHCARE S A ; Baxter International Inc Systems, methods and apparatuses for pumping cassette-based therapies
7384783, Apr 27 2004 Takeda Pharmaceutical Company Limited Stirred-tank reactor system
7619106, Oct 25 2002 Basell Polyolefine GmbH Preparation of partially hydrogenated rac-ansa-metallocene complexes
7731689, Feb 15 2007 Baxter International Inc; BAXTER HEALTHCARE S A Dialysis system having inductive heating
7744554, Dec 31 2002 Baxter International Inc; BAXTER HEALTHCARE S A Cassette alignment and integrity testing for dialysis systems
7998115, Feb 15 2007 Baxter International Inc; BAXTER HEALTHCARE S A Dialysis system having optical flowrate detection
8206338, Dec 31 2002 Baxter International Inc; BAXTER HEALTHCARE S A Pumping systems for cassette-based dialysis
8323231, Feb 10 2000 Baxter International, Inc. Method and apparatus for monitoring and controlling peritoneal dialysis therapy
8361023, Feb 15 2007 Baxter International Inc; BAXTER HEALTHCARE S A Dialysis system with efficient battery back-up
8545435, Jan 03 2002 Baxter International, Inc. Method and apparatus for providing medical treatment therapy based on calculated demand
8558964, Feb 15 2007 Baxter International Inc; BAXTER HEALTHCARE S A Dialysis system having display with electromagnetic compliance (“EMC”) seal
8870812, Feb 15 2007 Baxter International Inc; BAXTER HEALTHCARE S A Dialysis system having video display with ambient light adjustment
9474842, Feb 10 2000 Baxter International Inc. Method and apparatus for monitoring and controlling peritoneal dialysis therapy
9799274, Feb 15 2007 Baxter International Inc.; BAXTER HEALTHCARE SA Method of controlling medical fluid therapy machine brightness
Patent Priority Assignee Title
4769510, Nov 27 1984 Targor GmbH Process for the preparation of polyolefins
4871705, Jun 16 1988 EXXON CHEMICAL PATENTS INC , A CORP OF DE Process for production of a high molecular weight ethylene a-olefin elastomer with a metallocene alumoxane catalyst
4892851, Jul 15 1988 COSDEN TECHNOLOGY, INC , A CORP OF DE Process and catalyst for producing syndiotactic polyolefins
4931417, Nov 09 1987 Chisso Corporation; INSTITUTE OF PHYSICAL AND CHEMICAL RESEARCH, THE Transition-metal compound having a bis-substituted-cyclopentadienyl ligand of bridged structure
5017714, Mar 21 1988 Exxon Chemical Patents Inc. Silicon-bridged transition metal compounds
5087677, Jul 08 1989 Ticona GmbH Process for the preparation of cycloolefin polymers
5103030, Dec 18 1987 Targor GmbH Process for the preparation of a chiral stereorigid metallocene
5145819, Nov 12 1990 Basell Polyolefine GmbH 2-substituted disindenylmetallocenes, process for their preparation, and their use as catalysts in the polymerization of olefins
5243001, Nov 12 1990 Basell Polyolefine GmbH Process for the preparation of a high molecular weight olefin polymer
5276208, Nov 12 1990 Basell Polyolefine GmbH Metallocenes containing ligands of 2-substituted idenyl derivatives, process for their preparation, and their use as catalysts
5278264, Aug 26 1991 Basell Polyolefine GmbH Process for the preparation of an olefin polymer
5296434, Jun 18 1991 Basell Polyolefine GmbH Soluble catalyst systems for the preparation of polyalk-1-enes having high molecular weights
5324800, Jun 06 1983 Exxon Chemical Patents INC Process and catalyst for polyolefin density and molecular weight control
5329033, Aug 26 1991 Basell Polyolefine GmbH Process for the preparation of an olefin polymer
DE284708,
DE3726067,
DE3826075,
EP129368,
EP185918,
EP316155,
EP320762,
EP336128,
EP344887,
EP347129,
EP351392,
EP366290,
EP407870,
EP426643,
EP433990,
EP485821,
EP485823,
EP500005,
EP529908,
EP442725,
///
Executed onAssignorAssigneeConveyanceFrameReelDoc
Oct 17 1994Targor GmbH(assignment on the face of the patent)
Jan 05 1999Targor GmbHBasell Polypropylen GmbHCHANGE OF NAME SEE DOCUMENT FOR DETAILS 0141410551 pdf
Jul 29 2002Basell Polypropylen GmbHBasell Polyolefine GmbHMERGER SEE DOCUMENT FOR DETAILS 0141910800 pdf
Date Maintenance Fee Events
Oct 23 2002M1552: Payment of Maintenance Fee, 8th Year, Large Entity.
Oct 23 2002M1558: Surcharge, Petition to Accept Pymt After Exp, Unintentional.
Oct 23 2002PMFP: Petition Related to Maintenance Fees Filed.
Apr 03 2003PMFG: Petition Related to Maintenance Fees Granted.
Jun 23 2005M1553: Payment of Maintenance Fee, 12th Year, Large Entity.


Date Maintenance Schedule
Jun 05 20044 years fee payment window open
Dec 05 20046 months grace period start (w surcharge)
Jun 05 2005patent expiry (for year 4)
Jun 05 20072 years to revive unintentionally abandoned end. (for year 4)
Jun 05 20088 years fee payment window open
Dec 05 20086 months grace period start (w surcharge)
Jun 05 2009patent expiry (for year 8)
Jun 05 20112 years to revive unintentionally abandoned end. (for year 8)
Jun 05 201212 years fee payment window open
Dec 05 20126 months grace period start (w surcharge)
Jun 05 2013patent expiry (for year 12)
Jun 05 20152 years to revive unintentionally abandoned end. (for year 12)