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. 17, 2023

Filed:

Jul. 15, 2022
Applicants:

Lummus Technology Llc, Houston, TX (US);

Saudi Aramco Technologies Company, Dhahran, SA;

Chevron Lummus Global Llc, Richmond, CA (US);

Inventors:

Kareemuddin Shaik, Houston, TX (US);

Ujjal Mukherjee, Houston, TX (US);

Essam Abdullah Al-Sayed, Houston, TX (US);

Pedro Santos, Houston, TX (US);

Theodorus Maesen, Houston, TX (US);

Mazin Tamimi, Houston, TX (US);

Julie Chabot, Houston, TX (US);

Ibrahim Abba, Houston, TX (US);

Kandasamy Sundaram, Houston, TX (US);

Sami Barnawi, Houston, TX (US);

Ronald M. Venner, Houston, TX (US);

Assignees:

LUMMUS TECHNOLOGY LLC, Houston, TX (US);

Saudi Arabian Technology Company, Dhahran, SA;

Chevron Lummus Global LLC, Richmond, CA (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/06 (2006.01); B01D 3/06 (2006.01); B01J 19/24 (2006.01); C10L 1/08 (2006.01); C10G 45/26 (2006.01); C10G 45/32 (2006.01); C10G 45/44 (2006.01); C10G 49/22 (2006.01); C10G 65/12 (2006.01); C10G 9/36 (2006.01); C10G 47/30 (2006.01); C10G 49/02 (2006.01); C10G 21/00 (2006.01); C10G 47/26 (2006.01); C10G 55/04 (2006.01); B01D 19/00 (2006.01);
U.S. Cl.
CPC ...
C10G 69/06 (2013.01); B01J 19/245 (2013.01); C10G 9/36 (2013.01); C10G 21/003 (2013.01); C10G 45/26 (2013.01); C10G 45/32 (2013.01); C10G 45/44 (2013.01); C10G 47/26 (2013.01); C10G 47/30 (2013.01); C10G 49/02 (2013.01); C10G 49/22 (2013.01); C10G 55/04 (2013.01); C10G 65/12 (2013.01); C10L 1/08 (2013.01); B01D 3/06 (2013.01); B01D 19/0057 (2013.01); B01J 2219/0004 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1048 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/206 (2013.01); C10G 2300/301 (2013.01); C10G 2300/302 (2013.01); C10G 2300/308 (2013.01); C10G 2300/40 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4081 (2013.01); C10G 2300/807 (2013.01); C10G 2400/20 (2013.01); C10G 2400/22 (2013.01); C10G 2400/30 (2013.01);
Abstract

Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.


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