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:
Aug. 25, 2015

Filed:

Oct. 25, 2012
Applicant:

Shell Oil Company, Houston, TX (US);

Inventor:

Opinder Kishan Bhan, Katy, TX (US);

Assignee:

Shell Oil Company, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 23/88 (2006.01); B01J 23/883 (2006.01); C10G 45/08 (2006.01); B01J 37/04 (2006.01); B01J 37/28 (2006.01); B01J 35/00 (2006.01); B01J 35/10 (2006.01); B01J 37/02 (2006.01); B01J 23/76 (2006.01); B01J 23/84 (2006.01); B01J 23/85 (2006.01);
U.S. Cl.
CPC ...
B01J 23/883 (2013.01); B01J 35/002 (2013.01); B01J 35/1042 (2013.01); B01J 35/1061 (2013.01); B01J 37/0201 (2013.01); B01J 37/04 (2013.01); B01J 37/28 (2013.01); C10G 45/08 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01);
Abstract

A self activating catalyst for treating heavy hydrocarbon feedstocks that comprises a calcined particle comprising a co-mulled mixture made by co-mulling inorganic oxide powder, molybdenum trioxide powder, and a nickel compound and then forming the co-mulled mixture into a particle that is calcined to thereby provide the calcined particle. The calcined particle comprises from 1 to 10 weight percent molybdenum and nickel that is present in an amount such that the weight ratio of said nickel-to-molybdenum is less than 0.4. The calcined particle has a pore size distribution that contributes to the unique properties of the catalyst. The calcined particle and catalyst also exhibits a unique Raman spectrum. The self activating catalyst is activated when contacted under suitable process conditions with a heavy residue feedstock having high nickel, vanadium and sulfur concentrations.


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