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. 08, 2015

Filed:

Dec. 20, 2011
Applicants:

Julie Chabot, Novato, CA (US);

Bruce E. Reynolds, Martinez, CA (US);

Erin Maris, Alameda, CA (US);

Shuwu Yang, Richmond, CA (US);

Inventors:

Julie Chabot, Novato, CA (US);

Bruce E. Reynolds, Martinez, CA (US);

Erin Maris, Alameda, CA (US);

Shuwu Yang, Richmond, CA (US);

Assignee:

Chevron U.S.A. .Inc., San Ramon, CA (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 47/26 (2006.01); C10G 49/02 (2006.01); B01J 37/20 (2006.01); B01J 35/00 (2006.01); B01J 23/883 (2006.01); B01J 35/02 (2006.01); B01J 35/10 (2006.01); B01J 37/00 (2006.01); B01J 37/02 (2006.01); C10G 49/12 (2006.01);
U.S. Cl.
CPC ...
C10G 49/02 (2013.01); B01J 23/883 (2013.01); B01J 35/0006 (2013.01); B01J 35/023 (2013.01); B01J 35/1019 (2013.01); B01J 35/1023 (2013.01); B01J 35/1042 (2013.01); B01J 35/1047 (2013.01); B01J 35/1066 (2013.01); B01J 35/1076 (2013.01); B01J 37/0036 (2013.01); B01J 37/0201 (2013.01); B01J 37/20 (2013.01); C10G 49/12 (2013.01); B01J 35/1052 (2013.01); C10G 2300/208 (2013.01); C10G 2300/4056 (2013.01); C10G 2300/70 (2013.01); C10G 2300/708 (2013.01); C10G 2300/802 (2013.01);
Abstract

A method to upgrade heavy oil feedstock using an ebullated bed reactor and a novel catalyst system is provided. The ebullated bed reactor system includes two different catalyst with different characteristics: an expanded catalyst zone containing particulate catalyst having a particle size of greater than 0.65 mm; and a slurry catalyst having an average particle size ranging from 1 to 300 μm. The slurry catalyst is provided to the ebullated bed system containing the heavy oil feedstock, and entrained in the upflowing hydrocarbon liquid passing through the ebullated bed reaction zone. The slurry catalyst reduces the formation of sediment and coke precursors in the ebullating bed reactor system. The slurry catalyst is prepared from rework materials, which form a slurry catalyst in-situ upon mixing with the heavy oil feedstock.


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