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:
Oct. 18, 2016

Filed:

May. 12, 2008
Applicants:

Rashid Iqbal, Houston, TX (US);

Anshumali, Mobile, AL (US);

Odette Eng, Sugar Land, TX (US);

Phillip Niccum, Houston, TX (US);

Inventors:

Rashid Iqbal, Houston, TX (US);

Anshumali, Mobile, AL (US);

Odette Eng, Sugar Land, TX (US);

Phillip Niccum, Houston, TX (US);

Assignee:

Kellogg Brown & Root LLC, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 1/04 (2006.01); C10C 1/18 (2006.01); C10C 3/08 (2006.01); C10G 11/00 (2006.01); C10G 45/00 (2006.01); B01J 8/18 (2006.01); C10G 11/18 (2006.01); C10G 9/00 (2006.01); C10G 21/00 (2006.01); C10G 45/02 (2006.01); C10G 55/06 (2006.01); C10G 67/04 (2006.01); C10G 69/04 (2006.01); C10G 69/06 (2006.01);
U.S. Cl.
CPC ...
C10G 11/18 (2013.01); C10G 9/005 (2013.01); C10G 21/003 (2013.01); C10G 45/02 (2013.01); C10G 55/06 (2013.01); C10G 67/04 (2013.01); C10G 69/04 (2013.01); C10G 69/06 (2013.01);
Abstract

Disclosed is a process for the upgrading and demetallizing of heavy oils and bitumens. A crude heavy oil and/or bitumen feed is supplied to a solvent extraction processwherein DAO and asphaltenes are separated. The DAO is supplied to an FCC unithaving a low conversion activity catalyst for the removal of metals contained therein. The demetallized distillate fraction is supplied to a hydrotreaterfor upgrading and collected as a synthetic crude product stream. The asphaltene fraction can be supplied to a gasifierfor the recovery of power, steam and hydrogen, which can be supplied to the hydrotreateror otherwise within the process or exported. An optional coker unitcan be used to convert excess asphaltenes and/or decant oil to naphtha, distillate and gas oil, which can be supplied to the hydrotreater


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