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:
Dec. 30, 2025

Filed:

Sep. 06, 2023
Applicant:

King Fahd University of Petroleum and Minerals, Dhahran, SA;

Inventors:

Mohammad Mozahar Hossain, Dhahran, SA;

Majid Lasisi Balogun, Dhahran, SA;

Mohammed S. Ba-Shammakh, Dhahran, SA;

Shakeel Ahmed, Dhahran, SA;

Wasim Ullah Khan, Dhahran, SA;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01J 23/08 (2006.01); B01J 23/10 (2006.01); B01J 35/61 (2024.01); B01J 35/63 (2024.01); B01J 35/64 (2024.01); B01J 37/02 (2006.01); B01J 37/03 (2006.01); B01J 37/04 (2006.01); B01J 37/08 (2006.01); C07C 5/32 (2006.01);
U.S. Cl.
CPC ...
B01J 23/08 (2013.01); B01J 23/10 (2013.01); B01J 35/613 (2024.01); B01J 35/615 (2024.01); B01J 35/633 (2024.01); B01J 35/647 (2024.01); B01J 37/0205 (2013.01); B01J 37/0236 (2013.01); B01J 37/035 (2013.01); B01J 37/04 (2013.01); B01J 37/088 (2013.01); C07C 5/322 (2013.01); C07C 2523/08 (2013.01); C07C 2523/10 (2013.01);
Abstract

A method for producing propylene (CH) via oxidative dehydrogenation (ODH) of propane includes introducing a propane-containing feed gas stream into a reactor containing an alumina-supported GaO/LaOcatalyst comprising GaOparticles at least partially disposed on surfaces of a matrix comprising rough and irregular-sized LaOand alumina particles; passing the propane-containing feed gas stream through the reactor in contact with the alumina supported GaO/LaOcatalyst at a temperature of 500 to 600° C. to convert at least a portion of the propane to propylene (CH) and produce a propylene-containing gas stream leaving the reactor; and separating the propylene from the propylene-containing gas stream. The method has a propane conversion of up to 95% based on an initial weight of the propane in the propane-containing feed gas stream, and a propylene yield of up to 60% based on the propane conversion.


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