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:
Feb. 03, 2026

Filed:

Jan. 09, 2024
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Miao Sun, Dhahran, SA;

Lianhui Ding, Dhahran, SA;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 65/08 (2006.01); B01J 8/04 (2006.01); B01J 21/12 (2006.01); B01J 23/83 (2006.01); B01J 23/883 (2006.01); B01J 27/185 (2006.01); B01J 27/19 (2006.01); B01J 29/16 (2006.01); B01J 29/72 (2006.01); B01J 35/00 (2024.01); B01J 37/00 (2006.01);
U.S. Cl.
CPC ...
C10G 65/08 (2013.01); B01J 8/0453 (2013.01); B01J 8/0457 (2013.01); B01J 21/12 (2013.01); B01J 23/83 (2013.01); B01J 23/883 (2013.01); B01J 27/1853 (2013.01); B01J 27/19 (2013.01); B01J 29/166 (2013.01); B01J 29/7215 (2013.01); B01J 35/19 (2024.01); B01J 37/0009 (2013.01); B01J 2208/025 (2013.01); C10G 2300/1096 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/4018 (2013.01); C10G 2300/4025 (2013.01); C10G 2300/70 (2013.01); C10G 2400/30 (2013.01);
Abstract

Systems for upgrading pyrolysis oil include a first fixed-bed reactor having a first catalyst bed and a second catalyst bed. The first catalyst bed includes: a first treating catalyst containing alumina, binder, Mo, Ni, and P; a second treating catalyst made of AlO, SiO, ZrO, NiO, and WO; or both. The second catalyst bed includes mixed metal oxide catalyst. The first fixed-bed reactor contacts the pyrolysis oil with hydrogen in the presence of the treating catalyst and the mixed metal oxide catalyst to produce an intermediate stream comprising light aromatic compounds. The system includes a second fixed-bed reactor downstream that includes a mesoporous supported metal catalyst having nickel and tungsten on a mesoporous support. The second fixed-bed reactor contacts the intermediate stream with hydrogen in the presence of the mesoporous supported metal catalyst to produce a second reactor effluent comprising aromatic compounds having six to eight carbon atoms.


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