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:
Aug. 11, 2020

Filed:

May. 01, 2018
Applicants:

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

Korea Research Institute of Chemical Technology, Daejeon, KR;

Inventors:

Deuk Soo Park, Goyang-si, KR;

Ung Gi Hong, Seoul, KR;

Hyeongchan Ahn, Seoul, KR;

Won Choon Choi, Daejeon, KR;

Yong Ki Park, Seoul, KR;

Assignees:

SK GAS CO., LTD., Seongnam-si, Gyeonggi-Do, KR;

KOREA RESEARCH INSTITUTE OF CHEMICAL TECHNOLOGY, Daejeon, KR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 5/333 (2006.01); C07C 5/32 (2006.01); B01J 21/06 (2006.01); B01J 23/26 (2006.01); B01J 23/92 (2006.01); B01J 38/30 (2006.01);
U.S. Cl.
CPC ...
C07C 5/3332 (2013.01); B01J 21/066 (2013.01); B01J 23/26 (2013.01); B01J 23/92 (2013.01); B01J 38/30 (2013.01); C07C 2521/04 (2013.01); C07C 2521/06 (2013.01);
Abstract

Disclosed is an olefin production method which includes: (a) providing the regenerated catalyst and the hydrocarbon including not less than 90 wt % of LPG into Riser of Fast Fluidization Regime, and dehydrogenating in the presence of an alumina type catalyst; (b) separating an effluent from the dehydrogenation reaction into the catalyst and propylene mixture; (c) stripping to remove the hydrocarbon compound included in the catalyst separated at stage (b); (d) mixing the catalyst stripped at stage (c) with the gas including oxygen, and continuously regenerating it; (e) recycling the catalyst regenerated at stage (d) to stage (a), and providing it again into Riser; and (f) producing propylene product by cooling, compressing and separating propylene mixture of the reaction product separated at stage (b).


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