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. 19, 2026

Filed:

Jul. 20, 2023
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Miao Sun, Dhahran, SA;

Noor Al-Mana, Al Khobar, SA;

Lianhui Ding, Dhahran, SA;

Eman Zaki Albaher, Qatif, SA;

Guanghui Zhu, Dhahran, SA;

Ke Zhang, Winchester, MA (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 47/12 (2006.01); B01J 21/04 (2006.01); B01J 21/06 (2006.01); B01J 23/00 (2006.01); B01J 23/745 (2006.01); B01J 23/83 (2006.01); B01J 23/883 (2006.01); B01J 35/40 (2024.01); B01J 35/50 (2024.01); B01J 35/61 (2024.01); B01J 35/63 (2024.01); B01J 35/64 (2024.01); B01J 37/00 (2006.01); B01J 37/28 (2006.01); C10G 47/04 (2006.01); C10G 69/06 (2006.01);
U.S. Cl.
CPC ...
C10G 47/12 (2013.01); B01J 21/04 (2013.01); B01J 21/066 (2013.01); B01J 23/002 (2013.01); B01J 23/745 (2013.01); B01J 23/83 (2013.01); B01J 23/883 (2013.01); B01J 35/40 (2024.01); B01J 35/50 (2024.01); B01J 35/612 (2024.01); B01J 35/613 (2024.01); B01J 35/633 (2024.01); B01J 35/647 (2024.01); B01J 37/0009 (2013.01); B01J 37/28 (2013.01); C10G 47/04 (2013.01); C10G 69/06 (2013.01); C10G 2300/1096 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/4018 (2013.01); C10G 2300/70 (2013.01); C10G 2300/802 (2013.01); C10G 2400/30 (2013.01);
Abstract

Systems and method for upgrading pyrolysis oil to produce greater value aromatic compounds includes combining heavy pyrolysis oil and a diluent to produce the pyrolysis oil feed with least 30 wt. % multi-ring aromatic compounds boiling at greater than 360° C. The systems and methods include passing the pyrolysis oil feed to a fixed bed reactor having a hydrocracking catalyst that includes pellets having a particle size greater than or equal to 0.1 millimeter. The hydrocracking catalyst is a mixed metal oxide catalyst that includes a binder and mixed metal oxide particles or a supported metal oxide catalyst that includes molybdenum oxide and nickel oxide supported on a catalyst support material comprising a large-pore alumina. The methods may further include contacting the pyrolysis oil feed with the hydrogen in the presence of the hydrocracking catalyst at reaction conditions in the fixed bed reactor to produce a reaction effluent.


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