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:
Sep. 23, 2014

Filed:

Dec. 08, 2011
Applicants:

Stanley Nemec Milam, Houston, TX (US);

Michael Anthony Reynolds, Katy, TX (US);

Scott Lee Wellington, Bellaire, TX (US);

Easwar Santhosh Ranganathan, Houston, TX (US);

Win Sim Chan, Houston, TX (US);

Inventors:

Stanley Nemec Milam, Houston, TX (US);

Michael Anthony Reynolds, Katy, TX (US);

Scott Lee Wellington, Bellaire, TX (US);

Easwar Santhosh Ranganathan, Houston, TX (US);

Win Sim Chan, Houston, TX (US);

Assignee:

Shell Oil Company, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/04 (2006.01); C10G 47/06 (2006.01); C10G 47/26 (2006.01); C10G 47/02 (2006.01); C10G 11/18 (2006.01); B01J 27/051 (2006.01); C10G 45/04 (2006.01); B01J 27/047 (2006.01); C10G 65/12 (2006.01);
U.S. Cl.
CPC ...
C10G 69/04 (2013.01); C10G 2300/4012 (2013.01); C10G 47/06 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4006 (2013.01); C10G 47/26 (2013.01); C10G 47/02 (2013.01); C10G 11/182 (2013.01); C10G 2300/202 (2013.01); B01J 27/051 (2013.01); C10G 2400/02 (2013.01); C10G 45/04 (2013.01); B01J 27/047 (2013.01); C10G 2300/205 (2013.01); C10G 65/12 (2013.01);
Abstract

A process for treating a hydrocarbon-containing feedstock is provided in which a hydrocarbon-containing feedstock comprising at least 20 wt. % of heavy hydrocarbons is mixed with hydrogen and a non-acidic metal-containing catalyst at a temperature of 375° C. to 500° C. to produce a vapor comprising a first hydrocarbon-containing product. The vapor comprising the first hydrocarbon-containing product is separated from the mixture, and, apart from the mixture, the first hydrocarbon-containing product is contacted with hydrogen and a catalyst containing a Column 6 metal at a temperature of 260° C.-425° C. to produce a second hydrocarbon-containing product. The second hydrocarbon-containing product is separated into fractions, one of the fractions being a heavy hydrocarbon fraction comprised of hydrocarbons having a boiling point of at least 343° C. The heavy hydrocarbon fraction is then contacted with a fluidizable cracking catalyst at a temperature of at least 500° C.


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