The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Jul. 08, 2025

Filed:

Dec. 15, 2021
Applicant:

Dow Global Technologies Llc, Midland, MI (US);

Inventors:

Lin Luo, Lake Jackson, TX (US);

Yang Yang, Freeport, TX (US);

Adrianus Koeken, Terneuzen, NL;

Brien Stears, Seabrook, TX (US);

Luis Bollmann, Freeport, TX (US);

Andrzej Malek, Midland, MI (US);

Brian W. Goodfellow, Freeport, TX (US);

Assignee:

Dow Global Technologies LLC, Midland, MI (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 5/333 (2006.01); B01J 21/04 (2006.01); B01J 23/62 (2006.01); B01J 23/96 (2006.01); B01J 38/02 (2006.01); B01J 38/30 (2006.01);
U.S. Cl.
CPC ...
C07C 5/3337 (2013.01); B01J 21/04 (2013.01); B01J 23/62 (2013.01); B01J 23/96 (2013.01); B01J 38/02 (2013.01); B01J 38/30 (2013.01); C07C 2523/62 (2013.01);
Abstract

According to one or more embodiments of the present disclosure, a method for producing olefins includes contacting a hydrocarbon-containing feed with a catalyst in a reactor portion of a reactor system to form an olefin-containing effluent, separating at least a portion of the olefin-containing effluent from the catalyst, passing the catalyst to a catalyst-processing portion of the reactor system and processing the catalyst to produce a processed catalyst and a combustion gas, passing the processed catalyst from the catalyst-processing portion to the reactor portion, and introducing a combustion additive to the reactor system when the combustion gas comprises one or more hydrocarbons in an amount greater than 5% of an LFL of the combustion gas at a temperature and pressure of the catalyst processing portion. The catalyst may include from 1 ppmw to 150 ppmw platinum. The combustion additive may include from 150 ppmw to 1,000 ppmw platinum.


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