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:
May. 09, 2017

Filed:

Jul. 30, 2012
Applicants:

Everette Harris, Ivyland, PA (US);

Jeffrey Gendler, Richboro, PA (US);

Inventors:

Everette Harris, Ivyland, PA (US);

Jeffrey Gendler, Richboro, PA (US);

Assignee:

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

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/06 (2006.01); B01J 37/04 (2006.01); B01J 37/08 (2006.01); B01J 37/20 (2006.01); B01J 23/28 (2006.01); B01J 27/043 (2006.01); B01J 27/047 (2006.01); B01J 27/051 (2006.01); B01J 35/02 (2006.01); B01J 35/10 (2006.01); C10G 47/12 (2006.01); C10G 9/00 (2006.01); C10B 55/00 (2006.01); C10B 57/04 (2006.01);
U.S. Cl.
CPC ...
C10G 69/06 (2013.01); B01J 23/28 (2013.01); B01J 27/043 (2013.01); B01J 27/047 (2013.01); B01J 27/051 (2013.01); B01J 35/026 (2013.01); B01J 35/108 (2013.01); B01J 35/109 (2013.01); B01J 37/04 (2013.01); B01J 37/086 (2013.01); B01J 37/20 (2013.01); C10B 55/00 (2013.01); C10B 57/045 (2013.01); C10G 9/005 (2013.01); C10G 47/12 (2013.01); C10G 2300/206 (2013.01);
Abstract

Methods and systems for hydroprocessing heavy oil feedstocks to form upgraded material use a colloidal or molecular catalyst dispersed within heavy oil feedstock, pre-coking hydrocracking reactor, separator, and coking reactor. The colloidal or molecular catalyst promotes upgrading reactions that reduce the quantity of asphaltenes or other coke forming precursors in the feedstock, increase hydrogen to carbon ratio in the upgraded material, and decrease boiling points of hydrocarbons in the upgraded material. The methods and systems can be used to upgrade vacuum tower bottoms and other low grade heavy oil feedstocks. The result is one or more of increased conversion level and yield, improved quality of upgraded hydrocarbons, reduced coke formation, reduced equipment fouling, processing of a wider range of lower quality feedstocks, and more efficient use of supported catalyst if used with the colloidal or molecular catalyst, as compared to a conventional hydrocracking process or a conventional thermal coking process.


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