초록 ▼

The invention relates to a process for the preparation of polyolefins by polymerizing olefins of the formula CH 2 CHR in which R=H or C 1 -C 10 alkyl, on their own or as a mixture, if appropriate together with C 4 -C 12 α,ω-diolefins, in solvents, liquid monomers or the gas phase, at temperatures be

The invention relates to a process for the preparation of polyolefins by polymerizing olefins of the formula CH 2 CHR in which R=H or C 1 -C 10 alkyl, on their own or as a mixture, if appropriate together with C 4 -C 12 α,ω-diolefins, in solvents, liquid monomers or the gas phase, at temperatures between -50° and 200° C., using a catalyst system composed of a soluble, halogen-containing transition metal compound of the general formula ##EQU##(cyclopentadienyl) 2 Me R Hal in which R is cyclopentadienyl or a C 1 -C 6 alkyl radical or a halogen, in particular chlorine, Me is a transition metal, in particular zirconium, and Hal is a halogen, in particular chlorine, and a compound, containing aluminum, of the aluminoxane type having the general formulae ##EQU##Al 2 OR 4 (Al(R)--O) n for a linear aluminoxane and/or ##EQU##(Al(R)--O) n+2 for a cyclic aluminoxane, in which n is a number from 4 to 20 and R is a methyl or ethyl radical, preferably a methyl radical.

대표청구항 ▼

1. A process for the preparation of a polyolefin by polymerizing an olefin of the formula CH 2 CHR in which R=H or C 1 -C 10 alkyl, on its own or as a mixture, with other olefins or with C 4 -C 12 α,ω-diolefins, in solvents, liquid monomers or the gas phase, at temperatures between -50° and 200° C.,

1. A process for the preparation of a polyolefin by polymerizing an olefin of the formula CH 2 CHR in which R=H or C 1 -C 10 alkyl, on its own or as a mixture, with other olefins or with C 4 -C 12 α,ω-diolefins, in solvents, liquid monomers or the gas phase, at temperatures between -50° and 200° C., using a soluble, halogen-containing transition metal compound and aluminoxanes, which comprises carrying out the polymerization in the presence of a catalyst system composed of the following components: (a) bis-(cyclopentadienyl)-zirconium dichloride or bis-(cyclopentadienyl-zirconium monomethyl monochloride, and (b) a compound, containing aluminum, of the aluminoxane type having the general formulae ##EQU##Al 2 OR 4 (Al(R)--O) n for a linear aluminoxane and ##EQU##(Al(R)--O) n+2 for a cyclic aluminoxane, in which n is a number from 4 to 20 and R is a methyl or ethyl radical. 2. The process as claimed in claim 1, wherein (b) is methylaluminoxane. 3. The process as claimed in claim 1, wherein the polymerization of ethylene is carried out at transition metal concentrations from 10 -6 to 10 -8 mole/l. 4. The process as claimed in claim 1, wherein the polymerization is carried out with impure ethylene without increasing the catalyst concentration. 5. The process as claimed in claim 1, wherein the polymerization temperature is between 20° and 120° C. 6. The process as claimed in claim 1, wherein ethylene is copolymerized with propylene. 7. The process as claimed in claim 1, wherein the copolymerization of ethylene with other α-olefins is carried out. 8. A process for the preparation of a polyolefin by polymerizing at least one olefin of the formula CH 2 =CHR 1 in which R 1 =H or C 1 to C 5 alkyl, in solvents, liquid monomers or the gas phase, at temperatures between -50° and 200° C., which comprises carrying out the polymerization in the presence of a catalyst system comprising: (a) bis-(cyclopentadienyl)-zirconium dichloride or bis-(cyclopentadienyl)-zirconium monomethyl monochloride and (b) a compound of the aluminoxane type having the general formula ##EQU##Al 2 O(CH 3 ) 4 (Al[CH 3 ]--O) n for a linear aluminoxane and ##EQU##(Al[CH 3 ]--O) n+2 for a cyclic aluminoxane, in which n is a number from 4 to 20; wherein the aluminoxane concentration is 10 -8 to 10 -1 mole/l and the Zr concentration is 10 -6 to 10 -8 mole/l.