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. 14, 2021

Filed:

Feb. 28, 2018
Applicant:

Hydrocarbon Technology & Innovation, Llc, Lawrenceville, NJ (US);

Inventors:

David M. Mountainland, Princeton, NJ (US);

Brett M. Silverman, Salt Lake City, UT (US);

Michael A. Rueter, Plymouth Meeting, PA (US);

Lee Smith, Pleasant Grove, UT (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 47/00 (2006.01); C10G 47/02 (2006.01); C10G 49/26 (2006.01); C10G 65/00 (2006.01); C10G 75/04 (2006.01); C10G 49/12 (2006.01); B01J 8/18 (2006.01); B01J 8/24 (2006.01); B01J 27/04 (2006.01); B01J 35/00 (2006.01); B01J 35/02 (2006.01); B01J 37/04 (2006.01); B01J 37/08 (2006.01); C10G 47/30 (2006.01); C10G 47/36 (2006.01); C10G 75/00 (2006.01);
U.S. Cl.
CPC ...
C10G 47/02 (2013.01); B01J 8/1809 (2013.01); B01J 8/24 (2013.01); B01J 27/04 (2013.01); B01J 35/0006 (2013.01); B01J 35/023 (2013.01); B01J 37/04 (2013.01); B01J 37/08 (2013.01); C10G 47/30 (2013.01); C10G 47/36 (2013.01); C10G 49/12 (2013.01); C10G 49/26 (2013.01); C10G 65/00 (2013.01); C10G 75/00 (2013.01); C10G 75/04 (2013.01); B01J 2219/00247 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/206 (2013.01); C10G 2300/208 (2013.01); C10G 2300/301 (2013.01); C10G 2300/70 (2013.01);
Abstract

An ebullated bed hydroprocessing system is upgraded using a dual catalyst system that includes a heterogeneous catalyst and dispersed metal sulfide particles to produce less fouling sediment. The dual catalyst system more effectively converts sediment-forming precursors to produce sediment that is less fouling than sediment produced using only the heterogeneous catalyst and not the dispersed metal sulfide particles. The dual catalyst system provides for a lower rate of equipment fouling for a given sediment production rate and/or concentration. In some cases, sediment production rate and/or concentration can be maintained or increased while equipment fouling is reduced. In some cases, sediment production rate and/or concentration can be increased without increasing equipment fouling.


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