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US4871705A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for production of a high molecular weight ethylene a-olefin elastomer with a metallocene alumoxane catalyst

Assignee: ExxonMobil Chemical Patents Inc
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Filing: 1988-06-16
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Granted: 1989-10-03
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Expires: 2008-06-16
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Abstract

Abstract Disclosed is a process for preparing high molecular weight ethylene-α-olefin elastomers, preferably an ethylene-propylene elastomer, by liquid phase polymerization of the requisite monomers in the presence of a metallocene/alumoxane catalyst system. Preferably, the process is carried out as a slurry polymerization utilizing the metallocene/alumoxane catalyst in supported form on a silica gel support with the α-olefin monomer maintained in liquid state and used in excess to serve as a polymerization diluent. The metallocene component of the catalyst by which the process is practiced is of the formula: ##STR1## wherein M is zirconium, titanium or hafnium; each R 1 independently is a C 1 -C 20 linear, branched or cyclic alkyl group or a C 2 -C 4 cyclic alkylene group which forms a fused ring system group; R 2 is a C 1 -C 6 linear, branched or cyclic alkylene, a Si 1 -Si 2 alkyl substituted silanylene group or an alkyl substituted silaalkylene group; each X independently is an alkyl, aryl, halide, hydride or oxygen bridge of a zirconocene dimer; "y" is a number 2, 3 or 4, and "b" is a number 0 or 1. M is preferably zirconium. Most preferably, the supported zirconocene/alumoxane catalyst is prepolymerized with ethylene or another olefin to provide spherical, free-flowing catalyst particles which give free-flowing particulate elastomer product from the slurry polymerization.

Inventors

  • 👤 Elvin L. Hoel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 00:26
CPC Classifications
C; C08; C08F; C08F210/00; C08F210/16; C08F4/00; C08F4/42; C08F4/44; C08F4/60; C08F4/62; C08F4/64; C08F4/659; C08F4/65912; C08F4/65916; C08F4/6592; C08F4/65922; Y; Y10; Y10S; Y10S526/00; Y10S526/904; Y10S526/943

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 150 words
A prepolymerized catalyst for producing EPC elastomers in liquid olefin slurry polymerization, comprising: an inorganic support which has been dried and treated with an alumoxane followed by addition of zirconocene of structure: ##STR6## wherein each R 1 independently is a C 1 -C 20 linear, branched or cyclic alkyl group or a C 2 -C-- 4 cyclic alkylene group which forms a fused ring system group; R 2 is a C 1 -C 6 linear, branched or cyclic alkylene, a Si 1 -Si 2 alkyl substituted silanylene group or an alkyl substituted silaalkylene group; each X independently is a halide, hydride, an oxygen bridge of a zirconocene dimer, or a hydrocarbyl radical; "y" is a number 2, 3, or 4, and "b" is either 0 or 1; followed by a prepolymerization treatment with ethylene or an α-olefin to increase the weight of the catalyst by at least 50 wt. %.
Claim 2
Dependent Claim 150 words
A prepolymerized catalyst for producing EPC elastomers in liquid olefin slurry polymerization, comprising: an inorganic support which has been dried and treated with an alumoxane followed by addition of zirconocene of structure: ##STR6## wherein each R 1 independently is a C 1 -C 20 linear, branched or cyclic alkyl group or a C 2 -C-- 4 cyclic alkylene group which forms a fused ring system group; R 2 is a C 1 -C 6 linear, branched or cyclic alkylene, a Si 1 -Si 2 alkyl substituted silanylene group or an alkyl substituted silaalkylene group; each X independently is a halide, hydride, an oxygen bridge of a zirconocene dimer, or a hydrocarbyl radical; "y" is a number 2, 3, or 4, and "b" is either 0 or 1; followed by a prepolymerization treatment with ethylene or an α-olefin to increase the weight of the catalyst by at least 50 wt. %.
Claim 3
Dependent Claim 20 words
The prepolymerized catalyst of claim 1 wherein the inorganic support is a silica gel dried at 100° to 1000° C.
Claim 4
Dependent Claim 30 words
The prepolymerized catalyst of claim 2 wherein the alumoxane is methylalumoxane and the ratio with the silica gel is in the range of 1:1 to 1:10 on a weight basis.
Claim 5
Dependent Claim 22 words
The prepolymerized catalyst of claim 3 wherein the mole ratio of aluminum to zirconium is in the range of 1 to 500.
Claim 6
Dependent Claim 21 words
The prepolymerized catalyst of claim 4 wherein the prepolymerization weight gain is in the range of 50 to 500 wt. %.
Claim 7
Dependent Claim 12 words
The prepolymerized catalyst of claim 5 wherein the zirconocene is bis(tetrahydroindenyl)zirconium dichloride.
Claim 8
Dependent Claim 13 words
The prepolymerized catalyst of claim 5 wherein the zirconocene is dimethylsilanylene-bis(tetrahydroindenyl) zirconium dichloride.
Claim 9
Dependent Claim 12 words
The prepolymerized catalyst of claim 5 wherein the zirconocene, is ethylene-bis(tetrahydroindenyl)zirconium dichloride.
Claim 10
Dependent Claim 20 words
The prepolymerized catalyst of claims 6, 7 or 8 wherein the prepolymerized catalyst is washed with a hydrocarbon following prepolymerization.

References Cited (Backward Citations)

US4295991A Cited
EP0206794A1 Cited
US4701432A Cited
US4658078A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-10-02 1993-04-03 1993-10-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-10-02 1997-04-03 1997-10-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-10-02 2001-04-03 2001-10-03 $7700.00 Window Closed / Lapsed

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