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:
Nov. 12, 2019

Filed:

Nov. 17, 2017
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 7/00 (2006.01); C10G 7/06 (2006.01); C10G 47/00 (2006.01); C10G 47/32 (2006.01); C10G 69/14 (2006.01); C10G 63/06 (2006.01); C10G 35/04 (2006.01); B01D 3/10 (2006.01); B01D 3/14 (2006.01); C10G 67/00 (2006.01); C10G 69/00 (2006.01); C10G 69/06 (2006.01); C10G 69/08 (2006.01); C10G 9/36 (2006.01); C10G 21/00 (2006.01);
U.S. Cl.
CPC ...
C10G 63/06 (2013.01); B01D 3/10 (2013.01); B01D 3/14 (2013.01); C10G 7/00 (2013.01); C10G 7/06 (2013.01); C10G 9/36 (2013.01); C10G 21/00 (2013.01); C10G 35/04 (2013.01); C10G 47/00 (2013.01); C10G 67/00 (2013.01); C10G 69/00 (2013.01); C10G 69/06 (2013.01); C10G 69/08 (2013.01); C10G 69/14 (2013.01); C10G 2300/1037 (2013.01); C10G 2300/1059 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/06 (2013.01); C10G 2400/08 (2013.01); C10G 2400/16 (2013.01); C10G 2400/20 (2013.01); C10G 2400/30 (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 conversion of naphtha to chemical rich reformate. Feeds to the mixed feed steam cracker include light products from hydroprocessing zones 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. Chemical reformate from straight run naphtha streams is used as an additional feed to the aromatics extraction zone and or the mixed feed steam cracker. Feeds to the gas oil steam cracker include hydrotreated gas oil range intermediates from the vacuum gas oil hydroprocessing zone.


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