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. 19, 2019
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Ki-Hyouk Choi, Dhahran, SA;

Mohnnad H. Alabsi, Dhahran, SA;

Muneef F. Alqarzouh, Dhahran, SA;

Rakan S. Mubayedh, Alkhobar, SA;

Sung Ho Choi, Dhahran, SA;

Assignee:
Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/06 (2006.01); C10G 31/08 (2006.01); C10G 9/00 (2006.01); C10G 7/06 (2006.01);
U.S. Cl.
CPC ...
C10G 69/06 (2013.01); C10G 7/06 (2013.01); C10G 9/007 (2013.01); C10G 31/08 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/807 (2013.01);
Abstract

Embodiments of the disclosure provide a visbreaking system and method for upgrading heavy hydrocarbons. A heavy hydrocarbon feed is introduced to a furnace to produce a soaker feed stream. The soaker feed stream is introduced to a soaker to produce a soaker effluent stream. The soaker effluent stream is introduced to a fractionator to produce a visbreaker distillate stream and a visbreaker residue stream. The visbreaker residue stream and a water feed are introduced to a supercritical water reactor operated at supercritical conditions of water to produce an effluent stream. The effluent stream is introduced to a flash column to produce a gas phase stream including water and a liquid phase stream including water. A portion of the liquid phase stream and the heavy hydrocarbon feed is combined. Optionally, a portion of the gas phase stream and the heavy hydrocarbon feed is combined. Optionally, a portion of the gas phase stream is introduced to the fractionator.


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