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:
Sep. 13, 2022

Filed:

Dec. 04, 2019
Applicants:

SK Gas Co., Ltd., Seongnam-si, KR;

Korea Research Institute of Chemical Technology, Daejeon, KR;

Korea National University of Transportation Industry-academic Cooperation Foundation, Chungju-si, KR;

Inventors:

Yong Ki Park, Seoul, KR;

Won Choon Choi, Daejeon, KR;

Daesung Park, Daejeon, KR;

Hawon Park, Daejeon, KR;

Changyeol Song, Daejeon, KR;

Deuk Soo Park, Yongin-si, KR;

Ung Gi Hong, Seongnam-si, KR;

Miyoung Lee, Seoul, KR;

Sungwon Kim, Chungju-si, KR;

Chaeeun Yeo, Chungju-si, KR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 21/06 (2006.01); B01J 8/38 (2006.01); B01J 21/04 (2006.01); B01J 23/26 (2006.01); B01J 23/30 (2006.01); B01J 35/02 (2006.01); B01J 35/10 (2006.01); B01J 37/08 (2006.01); C07C 5/333 (2006.01);
U.S. Cl.
CPC ...
B01J 21/066 (2013.01); B01J 8/38 (2013.01); B01J 21/04 (2013.01); B01J 23/26 (2013.01); B01J 23/30 (2013.01); B01J 35/023 (2013.01); B01J 35/1014 (2013.01); B01J 35/1019 (2013.01); B01J 37/088 (2013.01); C07C 5/3332 (2013.01); C07C 2521/04 (2013.01); C07C 2521/06 (2013.01); C07C 2523/26 (2013.01); C07C 2523/30 (2013.01);
Abstract

Disclosed is a method of producing an olefin using a circulating fluidized bed process, including: (a) supplying a hydrocarbon mixture including propane and a dehydrogenation catalyst to a riser which is in a state of a fast fluidization regime, and thus inducing a dehydrogenation reaction; (b) separating an effluent from the dehydrogenation reaction into the catalyst and a propylene mixture; (c) stripping, in which a residual hydrocarbon compound is removed from the catalyst separated in step (b); (d) mixing the catalyst stripped in step (c) with a gas containing oxygen and thus continuously regenerating the catalyst; (e) circulating the catalyst regenerated in step (d) to step (a) and thus resupplying the catalyst to the riser; and (f) cooling, compressing, and separating the propylene mixture, which is a reaction product separated in step (b), and thus producing a propylene product.


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