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US4359562A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing ethylene polymers and copolymers by means of a supported catalyst of a chromium-hydrocarbon complex on an inorganic oxide carrier

Assignee: BASF SE
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Filing: 1981-07-17
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Granted: 1982-11-16
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Expires: 2001-07-17
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Abstract

Abstract A process for the preparation of ethylene homopolymers, and ethylene copolymers with minor amounts of higher α-monoolefins, by polymerizing the monomer or monomers by means of a supported catalyst (1) containing a chromium-hydrocarbon complex (1.2) on an inorganic oxide carrier (1.1), wherein (1) a supported catalyst is employed which contains (1.2) a chromium-hydrocarbon complex of the formula RCrACrR, where R is a cyclic and/or open-chain hydrocarbon, or hydrocarbon radical, of 2n and 2n+1 carbon atoms respectively and having from 1 to n non-cumulated double bonds, n being from 2 to 10, Cr is chromium and A is cyclooctatetraene, a divalent n-octatetraene radical or alkyl-substituted homologs thereof, on (1.1) a particular inorganic oxide carrier, with or without (2) a co-catalyst chosen from a particular group of alkyl-aluminum compounds. The process gives polymers having a particularly broad molecular weight distribution.

Inventors

  • 👤 Dieter Stein
  • 👤 Robert Bachl
  • 👤 Konrad Richter

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 14:05
CPC Classifications
C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 301 words
A process for the preparation of ethylene homopolymers and ethylene copolymers with minor amounts of C 3 -C 6 -α-monoolefins by polymerizing the monomer or monomers at from 30° to 200° C. under a pressure of from 0.1 to 200 bars, by means of a supported catalyst (1) which contains a chromium-hydrocarbon complex (1.2) on an inorganic oxide carrier (1.1), wherein (1) a supported catalyst is employed, which contains (1.1) on a finely divided, porous, inorganic oxide carrier, having a particle diameter of from 1 to 1,000 μm, a pore volume of from 0.3 to 3 cm 3 /g and a surface area of from 100 to 1,000 m 2 /g and which has the formula SiO 2 .aAl 2 O 3 , where a is a number from 0 to 2, (1.2) a chromium-hydrocarbon complex of the formula RCrACrR where R is a cyclic and/or open-chain hydrocarbon or hydrocarbon radical which contains 2n and 2n+1 carbon atoms respectively and from 1 to n non-cumulated double bonds, n being an integer from 2 to 10, Cr is chromium and A is cyclooctatetraene or a divalent n-octatetraene radical, which is unsubstituted or in which up to 8 hydrogen atoms of the cyclooctatetraene or n-octatetraene radical can be substituted by C 1 -C 4 -alkyl, (2) with or without a co-catalyst of the formula ##STR2## where X is chlorine, hydrogen, R' or OR', Y is R' and OR' and R' is C 1 -C 18 -alkyl, with the provisos that (i) the supported catalyst (1) contains from 0.01 to 10% by weight, calculated as chromium and based on carrier (1.1), of the complex compound (1.2) and (ii) that, where the co-catalyst is present, the atomic ratio of chromium in the supported catalyst (1) to aluminum in the co-catalyst (2) is up to 1:1,000.
Claim 2
Dependent Claim 301 words
A process for the preparation of ethylene homopolymers and ethylene copolymers with minor amounts of C 3 -C 6 -α-monoolefins by polymerizing the monomer or monomers at from 30° to 200° C. under a pressure of from 0.1 to 200 bars, by means of a supported catalyst (1) which contains a chromium-hydrocarbon complex (1.2) on an inorganic oxide carrier (1.1), wherein (1) a supported catalyst is employed, which contains (1.1) on a finely divided, porous, inorganic oxide carrier, having a particle diameter of from 1 to 1,000 μm, a pore volume of from 0.3 to 3 cm 3 /g and a surface area of from 100 to 1,000 m 2 /g and which has the formula SiO 2 .aAl 2 O 3 , where a is a number from 0 to 2, (1.2) a chromium-hydrocarbon complex of the formula RCrACrR where R is a cyclic and/or open-chain hydrocarbon or hydrocarbon radical which contains 2n and 2n+1 carbon atoms respectively and from 1 to n non-cumulated double bonds, n being an integer from 2 to 10, Cr is chromium and A is cyclooctatetraene or a divalent n-octatetraene radical, which is unsubstituted or in which up to 8 hydrogen atoms of the cyclooctatetraene or n-octatetraene radical can be substituted by C 1 -C 4 -alkyl, (2) with or without a co-catalyst of the formula ##STR2## where X is chlorine, hydrogen, R' or OR', Y is R' and OR' and R' is C 1 -C 18 -alkyl, with the provisos that (i) the supported catalyst (1) contains from 0.01 to 10% by weight, calculated as chromium and based on carrier (1.1), of the complex compound (1.2) and (ii) that, where the co-catalyst is present, the atomic ratio of chromium in the supported catalyst (1) to aluminum in the co-catalyst (2) is up to 1:1,000.

References Cited (Backward Citations)

GB1253063A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-11-15 1986-05-17 1986-11-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-11-15 1990-05-17 1990-11-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-11-15 1994-05-17 1994-11-16 $7700.00 Window Closed / Lapsed

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