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:
Mar. 20, 2018

Filed:

Apr. 18, 2013
Applicant:

Headwaters Heavy Oil, Llc, South Jordan, UT (US);

Inventors:

Roger K. Lott, Edmonton, CA;

Lap Keung Lee, West Windsor, NJ (US);

Assignee:

HEADWATERS HEAVY OIL, LLC, South Jordan, UT (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 47/06 (2006.01); C10G 47/26 (2006.01); B01J 8/08 (2006.01); C10G 45/16 (2006.01); C10G 45/56 (2006.01); B01J 8/22 (2006.01); C10G 67/08 (2006.01); C10G 65/02 (2006.01); C10G 49/00 (2006.01); C10G 49/12 (2006.01); C10G 45/04 (2006.01); C10G 45/34 (2006.01); C10G 45/46 (2006.01); C10G 65/00 (2006.01);
U.S. Cl.
CPC ...
C10G 47/06 (2013.01); B01J 8/08 (2013.01); B01J 8/22 (2013.01); B01J 8/226 (2013.01); C10G 45/04 (2013.01); C10G 45/16 (2013.01); C10G 45/34 (2013.01); C10G 45/46 (2013.01); C10G 45/56 (2013.01); C10G 47/26 (2013.01); C10G 49/005 (2013.01); C10G 49/12 (2013.01); C10G 65/00 (2013.01); C10G 65/02 (2013.01); C10G 67/08 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1033 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/202 (2013.01); C10G 2300/206 (2013.01); C10G 2300/4056 (2013.01); C10G 2300/70 (2013.01); C10G 2300/703 (2013.01); C10G 2300/802 (2013.01);
Abstract

A hydrocracking system is upgraded by modifying an existing ebullated bed initially utilizing a supported ebullated bed catalyst to thereafter utilize a dual catalyst system that includes metal sulfide catalyst particles and supported ebullated bed catalyst. The upgraded hydrocracking system achieves at least one of: (1) hydroprocess lower quality heavy oil; (2) increase conversion of higher boiling hydrocarbons that boil at 524° C. (975° F.) or higher; (3) reduce the concentration of supported ebullated bed catalyst required to operate an ebullated bed reactor at a given conversion level; and/or (4) proportionally convert the asphaltene fraction in heavy oil at the same conversion level as the heavy oil as a whole. The metal sulfide catalyst may include colloidal or molecular catalyst particles less than 1 micron in size and formed in situ within the heavy oil using a catalyst precursor well-mixed within the heavy oil and decomposed to form catalyst particles.


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