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. 14, 2020

Filed:

Jan. 02, 2018
Applicants:

Saudi Arabian Oil Company, Dhahran, SA;

King Fahd University of Petroleum & Minerals, Dhahran, SA;

Inventors:

Sulaiman Saleh Al-Khattaf, Dhahran, SA;

Arudra Palani, Dhahran, SA;

Tazul Islam Bhuiyan, Dhahran, SA;

Sohel Shaikh, Dhahran, SA;

Mohammad Naseem Akhtar, Dhahran, SA;

Abdullah M. Aitani, Al-Khobar, SA;

Mohammed A. Al-Yami, Dhahran, SA;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 6/04 (2006.01); C07C 4/06 (2006.01); B01J 21/08 (2006.01); B01J 35/10 (2006.01); B01J 29/70 (2006.01); B01J 23/30 (2006.01); B01J 29/18 (2006.01); B01J 35/00 (2006.01); B01J 35/02 (2006.01); B01J 29/40 (2006.01); C01B 37/02 (2006.01); B01J 8/04 (2006.01); B01J 29/00 (2006.01); B01J 29/03 (2006.01); B01J 29/035 (2006.01); B01J 29/78 (2006.01); B01J 37/02 (2006.01); C07C 6/06 (2006.01); B01J 29/48 (2006.01);
U.S. Cl.
CPC ...
B01J 29/70 (2013.01); B01J 8/04 (2013.01); B01J 21/08 (2013.01); B01J 23/30 (2013.01); B01J 29/005 (2013.01); B01J 29/035 (2013.01); B01J 29/0308 (2013.01); B01J 29/0341 (2013.01); B01J 29/18 (2013.01); B01J 29/40 (2013.01); B01J 29/78 (2013.01); B01J 35/002 (2013.01); B01J 35/0006 (2013.01); B01J 35/023 (2013.01); B01J 35/108 (2013.01); B01J 35/1019 (2013.01); B01J 35/1023 (2013.01); B01J 35/1042 (2013.01); B01J 35/1047 (2013.01); B01J 35/1061 (2013.01); B01J 37/0201 (2013.01); C01B 37/02 (2013.01); C07C 4/06 (2013.01); C07C 6/04 (2013.01); C07C 6/06 (2013.01); B01J 29/0358 (2013.01); B01J 29/48 (2013.01); B01J 35/109 (2013.01); B01J 35/1057 (2013.01); B01J 2229/20 (2013.01); C07C 2521/08 (2013.01); C07C 2523/30 (2013.01); C07C 2529/03 (2013.01); C07C 2529/035 (2013.01); C07C 2529/40 (2013.01); C07C 2529/48 (2013.01); C07C 2529/70 (2013.01); C07C 2529/78 (2013.01); Y02P 20/52 (2015.11);
Abstract

Embodiments of processes for producing propylene utilize a dual catalyst system comprising a mesoporous silica catalyst impregnated with metal oxide and a mordenite framework inverted (MFI) structured silica catalyst downstream of the mesoporous silica catalyst, where the mesoporous silica catalyst includes a pore size distribution of at least 2.5 nm to 40 nm and a total pore volume of at least 0.600 cm/g, and the MFI structured silica catalyst has a total acidity of 0.001 mmol/g to 0.1 mmol/g. The propylene is produced from the butene stream via metathesis by contacting the mesoporous silica catalyst and subsequent cracking by contacting the MFI structured silica catalyst.


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