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:
Mar. 26, 2024

Filed:

Jan. 03, 2023
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Sohel K Shaikh, Dhahran, SA;

Raed H Abudawoud, Khobar, SA;

Zhonglin Zhang, Dhahran, SA;

Munir D Khokhar, Dhahran, SA;

Furqan Aljumah, Dhahran, SA;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 69/06 (2006.01); B01J 19/18 (2006.01); C07C 1/22 (2006.01); C07C 4/04 (2006.01); C07C 4/06 (2006.01); C07C 5/05 (2006.01); C07C 6/04 (2006.01); C07C 41/06 (2006.01); C10G 51/02 (2006.01); C10G 51/06 (2006.01); C10G 65/10 (2006.01); C10G 65/12 (2006.01);
U.S. Cl.
CPC ...
C10G 69/06 (2013.01); B01J 19/1862 (2013.01); C07C 1/22 (2013.01); C07C 4/04 (2013.01); C07C 4/06 (2013.01); C07C 5/05 (2013.01); C07C 6/04 (2013.01); C07C 41/06 (2013.01); C10G 51/023 (2013.01); C10G 51/026 (2013.01); C10G 51/06 (2013.01); C10G 65/10 (2013.01); C10G 65/12 (2013.01); B01J 2219/0004 (2013.01); C10G 2300/1044 (2013.01); C10G 2400/20 (2013.01);
Abstract

Processes for producing olefins include integration of steam cracking with a dual catalyst metathesis process. The processes include steam cracking a hydrocarbon feed to form a cracking reaction effluent containing butenes, separating the cracking reaction effluent to produce a cracking C4 effluent including normal butenes, isobutene, and 1,3-butadiene, subjecting the cracking C4 effluent to selective hydrogenation to convert 1,3-butadiene in the cracking C4 effluent to normal butenes, removing isobutene from a hydrogenation effluent to produce a metathesis feed containing normal butenes, and contacting the metathesis feed with a metathesis catalyst and a cracking catalyst directly downstream of the metathesis catalyst to produce a metathesis reaction effluent. Contacting with the metathesis catalyst causes metathesis of normal butenes to produce ethylene, propene, and C5+ olefins, and contacting with the cracking catalyst causes C5+ olefins produced through metathesis to undergo cracking reactions to produce additional propene, ethylene, or both.


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