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US5043515A Expired / Lapsed US ⏱️ 0.0 years remaining

Ethylene oligomerization catalyst and process

Assignee: Shell USA Inc
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Filing: 1989-08-08
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Granted: 1991-08-27
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Expires: 2009-08-08
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Abstract

Abstract This invention relates to an oligomerization catalyst comprising a zirconocene and one or more alkyl aluminoxanes wherein the alkyl is selected from methyl, ethyl and mixtures thereof and the ratio of equivalents of methyl to ethyl in the product ranges from about 4 to about 0.25 and wherein the atom ratio of aluminum to zirconium ranges from about 1 to about 100. It further relates to the method for preparing the catalyst and the use of the catalyst in an oligomerization process. The catalyst is particularly suited for the oligomerization of ethylene.

Inventors

  • 👤 Lynn H. Slaugh
  • 👤 Galeon W. Schoenthal

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 01:31
CPC Classifications
B; B01; B01J; B01J31/00; B01J31/02; B01J31/12; B01J31/14; B01J31/143; B01J31/16; B01J31/22; B01J31/2282; B01J31/2295; C; C07; C07C; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/26; C07C2/32; C07C2/34; B01J2231/00; B01J2231/20; B01J2531/00; B01J2531/40; B01J2531/48; C07C2531/00; C07C2531/02; C07C2531/12; C07C2531/14; C07C2531/16; C07C2531/22; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/582; Y10; Y10S; Y10S526/00; Y10S526/943

Claims Analysis

Total Claims: 30
Claim 1
Independent Claim 59 words
An olefin oligomerization catalyst comprising the reaction product of a zirconocene and one or more alkyl aluminoxanes wherein alkyl is a mixture of methyl and ethyl groups, wherein the ratio of equivalents of methyl to ethyl ranges from about 4 to about 0.25, and wherein the atom ratio of aluminum to zirconium ranges from about 0.1 to about 100.
Claim 2
Dependent Claim 59 words
An olefin oligomerization catalyst comprising the reaction product of a zirconocene and one or more alkyl aluminoxanes wherein alkyl is a mixture of methyl and ethyl groups, wherein the ratio of equivalents of methyl to ethyl ranges from about 4 to about 0.25, and wherein the atom ratio of aluminum to zirconium ranges from about 0.1 to about 100.
Claim 3
Dependent Claim 19 words
The catalyst of claim 1 wherein the ratio of methyl to ethyl ranges from about 2 to about 0.33.
Claim 4
Dependent Claim 19 words
The catalyst of claim 2 wherein the ratio of methyl to ethyl ranges from about 1 to about 0.5.
Claim 5
Dependent Claim 54 words
The catalyst of any one of claims 1-3 wherein the zirconocene has the general formula (cyclopentadientyl) n ZrY 4-n wherein n is an integer ranging from 1 to 4, Y is selected from the group consisting of hydrogen, a C 1 -C 5 alkyl group, a C 6 -C 20 aryl group and halogen.
Claim 6
Dependent Claim 39 words
The catalyst of claim 4 wherein the zirconocene is selected from bis(cyclopentadienyl)zirconium dichloride, bis(cyclopentadienyl)zirconium methyl chloride, bis(cyclopentadienyl)zirconium dimethyl, bis(methylcyclopentadienyl)zirconium dichloride, bis(methylcyclopentadienyl)zirconium methyl chloride, bis(methylcyclopentadienyl)zirconium dimethyl, bis(pentamethylcyclopentadienyl)zirconium dichloride, bis(pentamethylcyclopentadienyl)zirconium methyl chloride, bis(pentamethylcyclopentadienyl)zirconium dimethyl, bis(n-butyl-cyclopentadienyl)zirconium dichloride, bis(n-butylcyclopentadienyl)zirconium methyl chloride, bis(n-butyl-cyclopentadienyl)zirconium dimethyl.
Claim 7
Dependent Claim 20 words
The catalyst of claim 4 wherein the atom ratio of aluminum to zirconium ranges from about 1 to about 20.
Claim 8
Dependent Claim 20 words
The catalyst of claim 6 wherein the atom ratio of aluminum to zirconium ranges from about 1 to about 10.
Claim 9
Dependent Claim 20 words
The catalyst of claim 7 wherein the atom ratio of aluminum to zirconium ranges from about 1 to about 5.
Claim 10
Dependent Claim 25 words
The catalyst of any one of claims 1-3 wherein the alkyl aluminoxane is prepared by hydrolyzing a mixture of trimethyl aluminum and triethyl aluminum compounds.
Claim 11
Dependent Claim 28 words
The catalyst of any one of claims 1-3 wherein the alkyl aluminoxane is prepared by separately hydrolyzing trimethyl aluminum and triethyl aluminum and mixing the resultant aluminoxanes together.
Claim 12
Dependent Claim 81 words
A process for oligomerizing olefins comprising ethylene which comprises contacting said olefins at a temperature ranging from about 100° to about 130° C. with a catalyst comprising the reaction product of a zirconocene and one or more alkyl aluminoxanes wherein alkyl is a mixture of methyl and ethyl groups, wherein the ratio of equivalents of methyl to ethyl ranges from about 4 to about 0.25, and wherein the atom ratio of aluminum to zirconium ranges from about 0.1 to about 100.
Claim 13
Dependent Claim 81 words
A process for oligomerizing olefins comprising ethylene which comprises contacting said olefins at a temperature ranging from about 100° to about 130° C. with a catalyst comprising the reaction product of a zirconocene and one or more alkyl aluminoxanes wherein alkyl is a mixture of methyl and ethyl groups, wherein the ratio of equivalents of methyl to ethyl ranges from about 4 to about 0.25, and wherein the atom ratio of aluminum to zirconium ranges from about 0.1 to about 100.
Claim 14
Dependent Claim 21 words
The process of claim 11 wherein the catalyst the ratio of methyl to ethyl ranges from about 2 to about 0.33.
Claim 15
Dependent Claim 22 words
The process of claim 12 wherein in the catalyst the ratio of methyl to ethyl ranges from about 1 to about 0.5.
Claim 16
Dependent Claim 16 words
The process of claim 11 wherein the temperature ranges from about 110° to about 125° C.
Claim 17
Dependent Claim 16 words
The process of claim 11 wherein the temperature ranges from about 115° to about 120° C.
Claim 18
Dependent Claim 16 words
The process of claim 12 wherein the temperature ranges from about 110° to about 125° C.
Claim 19
Dependent Claim 16 words
The process of claim 12 wherein the temperature ranges from about 115° to about 120° C.
Claim 20
Dependent Claim 16 words
The process of claim 13 wherein the temperature ranges from about 110° to about 125° C.
Claim 21
Dependent Claim 16 words
The process of claim 13 wherein the temperature ranges from about 115° to about 120° C.
Claim 22
Dependent Claim 25 words
The process of any one of claims 11-19 wherein the olefins being oligomerized additionally comprise one or more C 3 to C 10 alpha olefins.
Claim 23
Dependent Claim 55 words
The process of any one of claims 11-19 wherein in the catalyst the zirconocene has the general formula (cyclopentadienyl)n-ZrY 4-n wherein n is an integer ranging from 1 to 4, Y is selected from the group consisting of hydrogen, a C 1 -C 5 alkyl group, a C 6 -C 20 aryl group and halogen.
Claim 24
Dependent Claim 42 words
The process of claim 21 wherein in the catalyst the zirconocene is selected from bis(cyclopentadienyl)zirconium dichloride, bis(cyclopentadienyl)zirconium methyl chloride, bis(cyclopentadienylzirconium dimethyl, bis(methylcyclopentadienyl)zirconium dichloride, bis(methylcyclopentadienyl)zirconium methyl chloride, bis(methylcyclopentadienyl)zirconium dimethyl, bis(pentamethylcyclopentadienyl)zirconium dichloride, bis(pentamethylcyclopentadienyl)zirconium methyl chloride, bis(pentamethylcyclopentadienyl)zirconium dimethyl, bis(n-butyl-cyclopentadienyl)zirconium dichloride, bis(n-butylcyclopentadienyl)zirconium methyl chloride, bis(n-butylcyclopentadienyl)zirconium dimethyl.
Claim 25
Dependent Claim 23 words
The process of claim 21 wherein in the catalyst the atom ratio of aluminum to zirconium ranges from about 1 to about 20.
Claim 26
Dependent Claim 23 words
The process of claim 23 wherein in the catalyst the atom ratio of aluminum to zirconium ranges from about 1 to about 10.
Claim 27
Dependent Claim 23 words
The process of claim 24 wherein in the catalyst the atom ratio of aluminum to zirconium ranges from about 1 to about 5.
Claim 28
Dependent Claim 28 words
The process of any one of claims 11-19 wherein in the catalyst the alkyl aluminoxane is prepared by hydrolyzing a mixture of trimethyl aluminum and triethyl aluminum compounds.
Claim 29
Dependent Claim 31 words
The process of any one of claims 11-19 wherein in the catalyst the alkyl aluminoxane is prepared by separately hydrolyzing trimethyl aluminum and triethyl aluminum and mixing the resultant aluminoxanes together.
Claim 30
Dependent Claim 25 words
The process of any one of claims 11-19 wherein the olefins being oligomerized additionally comprise one or more C 3 to C 10 alpha olefins.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1994-08-26 1995-02-25 1995-08-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-08-26 1999-02-25 1999-08-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-08-26 2003-02-25 2003-08-27 $7700.00 Window Closed / Lapsed

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