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. 24, 2011

Filed:

May. 26, 2010
Applicants:

Oleg Mironov, Hercules, CA (US);

Alexander E. Kuperman, Orinda, CA (US);

Jaime Lopez, Benicia, CA (US);

Axel Brait, San Rafael, CA (US);

Bruce Reynolds, Martinez, CA (US);

Kaidong Chen, Albany, CA (US);

Inventors:

Oleg Mironov, Hercules, CA (US);

Alexander E. Kuperman, Orinda, CA (US);

Jaime Lopez, Benicia, CA (US);

Axel Brait, San Rafael, CA (US);

Bruce Reynolds, Martinez, CA (US);

Kaidong Chen, Albany, CA (US);

Assignee:

Other;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 21/00 (2006.01); B01J 31/00 (2006.01); B01J 27/24 (2006.01); B01J 27/04 (2006.01);
U.S. Cl.
CPC ...
Abstract

A hydroprocessing bulk catalyst is provided. A process to prepare hydroprocessing bulk catalysts is also provided. The hydroprocessing catalyst has the formula (M)(L)(S)(C)(H)(O)(N), wherein M is at least one group VIB metal; promoter metal L is optional and if present, L is at least one Group VIII non-noble metal; t, u, v, w, x, y, z representing the total charge for each of the components (M, L, S, C, H, O and N, respectively); ta+ub+vd+we+xf+yg+zh=0; 0=<b; and 0=<b/a=<5, (a+0.5b)<=d<=(5a+2b), 0<=e<=11(a+b), 0<=f<=7(a+b), 0<=g<=5(a+b), 0<=h<=0.5(a+b). The catalyst has an X-ray powder diffraction pattern with at least one broad diffraction peak at any of Bragg angles: 8 to 18°, 32 to 40°, and 55 to 65° (from 0 to 70° 2-θ scale). In one embodiment, the catalyst is prepared by sulfiding at least one Group VIB metal compound and optionally at least one group VIII metal compound with a sulfiding agent forming a catalyst precursor; and mixing the catalyst precursor with a hydrocarbon compound to form the hydroprocessing catalyst composition.


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