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Process for producing tertiary-butylstyrene

Assignee: El Paso Products Co
•
Filing: 1980-01-29
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Granted: 1981-09-22
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Expires: 2000-01-29
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Abstract

Abstract This invention provides an improved oxydehydrogenation process for the production of tertiary-butylstyrene which involves the contacting of a vapor phase mixture of tertiary-butylethylbenzene and oxygen with a novel coprecipitated nickel-zirconium phosphate or nickel-zirconium-cerium phosphate catalyst composition. The tertiary-butylstyrene is produced with a high conversion selectivity, and concomitantly there is little or no dialkenylbenzene byproducts produced.

Inventors

  • 👤 Glen F. Crum
  • 👤 Samuel J. Paton

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 18:58
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/14; B01J27/185; B01J27/1853; C; C07; C07C; C07C5/00; C07C5/42; C07C5/48

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 101 words
A process for the production of tertiary-butylstyrene under moderate oxydehydrogenation conditions which comprises contacting a feed mixture of tertiary-butylethylbenzene and oxygen with a coprecipitated nickel-zirconium-cerium phosphate catalyst, wherein the cerium metal is in the plus three valence state, and the nickel, zirconium and cerium metal elements, respectively, are present in the catalyst in an atomic ratio of about 5-20:1:1 and the phosphate component is present in a sufficient quantity to satisfy the valences of the metal elements, and wherein the conversion selectivity to tertiary-butylstyrene is at least 80 mole percent, and the conversion selectivity to divinylbenzene is essentially zero mole percent.
Claim 2
Dependent Claim 101 words
A process for the production of tertiary-butylstyrene under moderate oxydehydrogenation conditions which comprises contacting a feed mixture of tertiary-butylethylbenzene and oxygen with a coprecipitated nickel-zirconium-cerium phosphate catalyst, wherein the cerium metal is in the plus three valence state, and the nickel, zirconium and cerium metal elements, respectively, are present in the catalyst in an atomic ratio of about 5-20:1:1 and the phosphate component is present in a sufficient quantity to satisfy the valences of the metal elements, and wherein the conversion selectivity to tertiary-butylstyrene is at least 80 mole percent, and the conversion selectivity to divinylbenzene is essentially zero mole percent.
Claim 3
Dependent Claim 23 words
A process in accordance with claim 1 wherein the feed mixture contains between about 0.2-5 moles of molecular oxygen per mole of tertiary-butylethylbenzene.
Claim 4
Dependent Claim 16 words
A process in accordance with claim 1 wherein the feed mixture contains a gaseous inert diluent.
Claim 5
Dependent Claim 23 words
A process in accordance with claim 1 wherein the feed mixture contains nitrogen and/or carbon dioxide and/or steam as a gaseous inert diluent.
Claim 6
Dependent Claim 28 words
A process in accordance with claim 1 wherein the contact time between the feed stream and the catalyst is in the range between about 0.5 and 20 seconds.

References Cited (Backward Citations)

US3207805A Cited
US3403192A Cited
US3733327A Cited
US3923916A Cited
US3935126A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-09-21 1985-03-23 1985-09-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-09-21 1989-03-23 1989-09-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-09-21 1993-03-23 1993-09-22 $7700.00 Window Closed / Lapsed

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