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:
Jan. 05, 2016

Filed:

Mar. 20, 2013
Applicants:

Ibrahim A. Abba, Dhahran, SA;

Raheel Shafi, Dhahran, SA;

Abdennour Bourane, Ras Tanura, SA;

Essam Sayed, Al-Khobar, SA;

Abdul Rahman Zafer Akhras, Dhahran, SA;

Inventors:

Ibrahim A. Abba, Dhahran, SA;

Raheel Shafi, Dhahran, SA;

Abdennour Bourane, Ras Tanura, SA;

Essam Sayed, Al-Khobar, SA;

Abdul Rahman Zafer Akhras, Dhahran, SA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/06 (2006.01); C10G 51/06 (2006.01); C10G 51/04 (2006.01); C10G 45/00 (2006.01); C10G 47/00 (2006.01); C10G 51/02 (2006.01); C10G 55/04 (2006.01); C10G 55/06 (2006.01); C10G 69/04 (2006.01); C10G 9/16 (2006.01); C10G 11/00 (2006.01); C10G 49/00 (2006.01); C10G 67/10 (2006.01); C10G 69/00 (2006.01); C10G 9/00 (2006.01); C10G 9/14 (2006.01);
U.S. Cl.
CPC ...
C10G 69/06 (2013.01); C10G 9/16 (2013.01); C10G 11/00 (2013.01); C10G 45/00 (2013.01); C10G 47/00 (2013.01); C10G 49/007 (2013.01); C10G 51/02 (2013.01); C10G 51/04 (2013.01); C10G 51/06 (2013.01); C10G 55/04 (2013.01); C10G 55/06 (2013.01); C10G 67/10 (2013.01); C10G 69/00 (2013.01); C10G 69/04 (2013.01); C10G 2300/201 (2013.01); C10G 2300/308 (2013.01); C10G 2400/20 (2013.01); C10G 2400/22 (2013.01); C10G 2400/30 (2013.01);
Abstract

An integrated hydrotreating, steam pyrolysis and catalytic cracking process for the production of olefins and aromatic petrochemicals from a crude oil feedstock is provided. Crude oil and hydrogen are charged to a hydroprocessing zone under conditions effective to produce a hydroprocessed effluent, which is thermally cracked in the presence of steam in a steam pyrolysis zone to produce a mixed product stream. Heavy components are catalytically cracked, which are derived from one or more of the hydroprocessed effluent, a heated stream within the steam pyrolysis zone, or the mixed product stream catalytically cracking. Catalytically cracked products are produced, which are combined with the mixed product stream and the combined stream is separated, and olefins and aromatics are recovered as product streams.


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