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. 20, 2020

Filed:

Aug. 29, 2019
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Mohammed Saeed Al-Ghamdi, Dammam, SA;

Bader BaHammam, Dammam, SA;

Naif Al Osaimi, Dammam, SA;

Sami Barnawi, Dammam, SA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 67/16 (2006.01); C10G 47/02 (2006.01); C10G 69/08 (2006.01); B01D 3/14 (2006.01); C10G 7/06 (2006.01); C10G 69/06 (2006.01); C10G 21/00 (2006.01); C10G 9/36 (2006.01); C10G 47/00 (2006.01);
U.S. Cl.
CPC ...
C10G 67/16 (2013.01); B01D 3/143 (2013.01); C10G 7/06 (2013.01); C10G 9/36 (2013.01); C10G 21/00 (2013.01); C10G 47/00 (2013.01); C10G 47/02 (2013.01); C10G 69/06 (2013.01); C10G 69/08 (2013.01); C10G 2300/1074 (2013.01); C10G 2300/1077 (2013.01); C10G 2400/16 (2013.01);
Abstract

Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking and gas oil steam cracking. Feeds to the mixed feed steam cracker include one or more naphtha fractions from hydroprocessing zones within the battery limits, including vacuum residue hydrocracking, within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline aromatics extraction zone within the battery limits. Feeds to the gas oil steam cracker include gas oil range intermediates from the vacuum gas oil hydroprocessing zone and the vacuum residue hydrocracking zone.


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