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. 27, 2016

Filed:

May. 09, 2014
Applicant:

Uop Llc, Des Plaines, IL (US);

Inventors:

Trung Pham, Mount Prospect, IL (US);

Lev Davydov, Northbrook, IL (US);

Lance Awender Baird, Prospect Heights, IL (US);

Assignee:

UOP LLC, Des Plaines, IL (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 8/26 (2006.01); C10G 55/00 (2006.01); C10G 51/06 (2006.01); C10G 69/00 (2006.01); C10G 3/00 (2006.01);
U.S. Cl.
CPC ...
B01J 8/26 (2013.01); C10G 3/42 (2013.01); C10G 51/06 (2013.01); C10G 55/00 (2013.01); C10G 69/00 (2013.01); B01J 2208/00991 (2013.01); C10G 2300/1014 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/4056 (2013.01); Y02P 30/20 (2015.11);
Abstract

Methods and apparatuses are provided for cracking a hydrocarbon. The method includes contacting a first hydrocarbon stream with a first cracking catalyst at a first cracking temperature in a first riser to produce a first riser effluent and a first spent catalyst. A second hydrocarbon stream is contacted with a second cracking catalyst at a second cracking temperature in a second riser to produce a second riser effluent and a second spent catalyst, where the second cracking temperature is less than the first cracking temperature. The first riser effluent and the second riser effluent are combined to produce a mixed riser effluent, and the mixed riser effluent is fractionated in a fractionation zone to produce a light cycle oil. The first spent catalyst and the second spent catalyst are combined in a reactor to produce a mixed spent catalyst.


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