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:
Oct. 19, 2021

Filed:

Dec. 27, 2019
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Ki-Hyouk Choi, Dhahran, SA;

Ali S. Alnasir, Dhahran, SA;

Emad N. Shafei, Dhahran, SA;

Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 55/06 (2006.01); C10G 55/00 (2006.01); B01J 19/24 (2006.01); B01J 3/00 (2006.01); C10L 1/06 (2006.01); B01D 3/10 (2006.01); B01D 3/06 (2006.01);
U.S. Cl.
CPC ...
C10G 55/06 (2013.01); B01J 3/008 (2013.01); B01J 19/245 (2013.01); C10G 55/00 (2013.01); C10L 1/06 (2013.01); B01D 3/06 (2013.01); B01D 3/10 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1074 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/202 (2013.01); C10G 2300/206 (2013.01); C10G 2300/308 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/805 (2013.01); C10G 2400/02 (2013.01); C10G 2400/20 (2013.01); C10G 2400/22 (2013.01); C10L 2200/0423 (2013.01); C10L 2270/023 (2013.01); C10L 2290/543 (2013.01);
Abstract

Embodiments of the disclosure provide a system and method for producing light olefins from a crude oil. A crude oil feed is introduced to a crude distillation unit to produce a distillate fraction and a residue fraction. The distillate fraction is introduced to a non-catalytic steam cracker to produce a light olefin fraction and a pyrolysis oil fraction. The residue fraction is introduced to a supercritical water reactor to produce an effluent stream. The effluent stream is introduced to a flash separator to produce a gas phase fraction and a liquid phase fraction. The gas phase fraction is introduced to a catalytic steam cracker to produce a light olefin fraction and a pyrolysis oil fraction. Optionally, the residue fraction is introduced to a vacuum distillation unit to produce a light vacuum gasoil fraction, a heavy vacuum gasoil fraction, and a vacuum residue fraction. The vacuum residue fraction is introduced to a solvent deasphalting unit to produce a deasphalted oil and a pitch fraction. The deasphalted oil fraction, optionally combined with the heavy vacuum gasoil fraction, can be introduced to the supercritical water reactor in lieu of the residue fraction.


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