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:
Nov. 25, 2014

Filed:

Mar. 20, 2012
Applicants:

April D. Ross, Beaumont, TX (US);

Thomas R. Halbert, Baton Rouge, LA (US);

William J. Novak, Bedminster, NJ (US);

John P. Greeley, Gaithersburg, MD (US);

Inventors:

April D. Ross, Beaumont, TX (US);

Thomas R. Halbert, Baton Rouge, LA (US);

William J. Novak, Bedminster, NJ (US);

John P. Greeley, Gaithersburg, MD (US);

Assignee:
Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 45/08 (2006.01); C10G 45/04 (2006.01); C10G 65/04 (2006.01); B01J 21/08 (2006.01); C10G 69/04 (2006.01); B01J 35/10 (2006.01); B01J 23/882 (2006.01);
U.S. Cl.
CPC ...
C10G 65/04 (2013.01); B01J 35/1047 (2013.01); B01J 23/882 (2013.01); C10G 45/08 (2013.01); B01J 21/08 (2013.01); B01J 35/1061 (2013.01); C10G 69/04 (2013.01); C10G 2300/1044 (2013.01); B01J 35/1042 (2013.01); C10G 2300/202 (2013.01);
Abstract

The invention includes a hydrotreating method for increased CO content comprising: contacting an olefinic naphtha feedstream with a hydrogen-containing treat gas stream and a hydrotreating catalyst in a reactor under hydrotreating conditions sufficient to at least partially hydrodesulfurize and/or hydrodenitrogenate the feedstream, wherein the feedstream and the hydrogen-containing treat gas stream collectively have greater than 10 vppm CO content and/or wherein the reactor inlet sees an average CO concentration of greater than 10 vppm, wherein the hydrotreating catalyst comprises a catalyst having cobalt and molybdenum disposed on a silica-based support, and wherein the hydrotreating conditions are selected such that the catalyst has a relative HDS activity at least 10% greater than an identical catalyst under identical conditions except for a collective CO content of the feedstream and/or hydrogen-containing treat gas being <10 vppm and/or a reactor inlet CO content <10 vppm.


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