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:
May. 03, 2016

Filed:

Feb. 15, 2013
Applicant:

Exxonmobil Chemical Patents Inc., Baytown, TX (US);

Inventors:

S. Mark Davis, Humble, TX (US);

Richard C. Stell, Houston, TX (US);

Jiunn-Shyan Liou, Bridgewater, NJ (US);

Stephen H. Brown, Annandale, NJ (US);

Paul F. Keusenkothen, Houston, TX (US);

Arthur R. Di Nicolantonio, Seabrook, TX (US);

John J. Waldrop, Kingwood, TX (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 8/18 (2006.01); B01J 10/00 (2006.01); C10B 55/10 (2006.01); C10G 9/00 (2006.01); C10G 9/36 (2006.01); C10G 51/02 (2006.01); C10B 55/00 (2006.01); B01J 19/00 (2006.01); B01J 19/24 (2006.01); B04C 7/00 (2006.01); B01D 21/26 (2006.01); B01D 45/12 (2006.01); C10G 9/34 (2006.01); C10G 51/00 (2006.01);
U.S. Cl.
CPC ...
B01J 10/005 (2013.01); C10B 55/00 (2013.01); C10B 55/10 (2013.01); C10G 9/005 (2013.01); C10G 9/007 (2013.01); C10G 9/36 (2013.01); C10G 51/023 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/807 (2013.01); C10G 2400/20 (2013.01); C10G 2400/30 (2013.01);
Abstract

This invention relates to a process and system for cracking hydrocarbon feedstock containing vacuum resid comprising: (a) subjecting a vacuum resid to a first thermal conversion in a thermal conversion reactor (such as delayed coker, fluid coker, Flexicoker™, visbreaker and catalytic hydrovisbreaker) where at least 30 wt % of the vacuum resid is converted to material boiling below 1050° F. (566° C.); (b) introducing said thermally converted resid to a vapor/liquid separator, said separator being integrated into a steam cracking furnace, to form a vapor phase and liquid phase; (c) passing said vapor phase to the radiant furnace in said steam cracking furnace; and (d) recovering at least 30 wt % olefins from the material exiting the radiant furnace (based upon the weight of the total hydrocarbon material exiting the radiant furnace).


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