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. 01, 2026

Filed:

Sep. 06, 2024
Applicant:

Chevron U.s.a. Inc., San Ramon, CA (US);

Inventors:

Huping Luo, Moraga, CA (US);

Xiaoying Ouyang, El Cerrito, CA (US);

Christopher Declan Lane, Kensington, CA (US);

Assignee:

CHEVRON U.S.A. INC., San Ramon, CA (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 11/18 (2006.01); B01J 8/28 (2006.01); B01J 38/30 (2006.01);
U.S. Cl.
CPC ...
C10G 11/182 (2013.01); B01J 8/28 (2013.01); C10G 11/185 (2013.01); B01J 38/30 (2013.01); B01J 2208/00371 (2013.01); C10G 2300/1025 (2013.01); C10G 2300/1081 (2013.01); C10G 2300/703 (2013.01);
Abstract

A fluidized bed reactor system including a fluidized bed reactor configured to receive a heated light hydrocarbon feed stream flowing upwards and a heated regenerated catalyst at a temperature sufficient to crack the heated light hydrocarbon feed stream to produce a product effluent stream containing hydrogen and spent catalyst having coke deposits, a catalyst regeneration unit operatively connected to a bottom portion of the fluidized bed reactor, the catalyst regeneration unit being configured to receive the spent catalyst flowing downwards and combust the coke deposits to produce the heated regenerated catalyst and a heated gas effluent for generating the heated light hydrocarbon feed stream, and a riser externally attached to the fluidized bed reactor and the catalyst regeneration unit, the riser being configured to receive the heated regenerated catalyst and a gas-based stream to flow the heated regenerated catalyst upwards to the fluidized bed reactor.


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