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:
Nov. 11, 2014

Filed:

Aug. 21, 2009
Applicants:

Keith H. Kuechler, Friendswood, TX (US);

Jennifer L. Bancroft, Houston, TX (US);

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

Robert D. Strack, Houston, TX (US);

Inventors:

Keith H. Kuechler, Friendswood, TX (US);

Jennifer L. Bancroft, Houston, TX (US);

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

Robert D. Strack, Houston, TX (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/06 (2006.01); C10G 9/38 (2006.01); C10G 45/00 (2006.01);
U.S. Cl.
CPC ...
C10G 69/06 (2013.01); C10G 2300/42 (2013.01); C10G 2300/107 (2013.01); C10G 9/38 (2013.01); C10G 2300/301 (2013.01); C10G 2300/1059 (2013.01); C10G 45/00 (2013.01);
Abstract

In one aspect, the invention includes in a process for cracking a hydrocarbon feedstock comprising: a) feeding a hydrocarbon feedstock containing at least 1 wt % of resid components having boiling points of at least 500° C. to a furnace convection section to heat the feedstock; b) flashing the heated feedstock in a first flash separation vessel to create a first overhead stream and a first bottoms liquid stream; c) hydrogenating at least a portion of the first bottoms liquid stream to create a hydrogenated bottoms stream; d) flashing the hydrogenated bottoms stream in a second flash separation vessel to create a second overhead stream and a second bottoms liquid stream; e) cracking the first overhead stream and the second overhead stream in a cracking furnace to produce a pyrolysis effluent stream. In other embodiments, the process further comprises heating the hydrocarbon feedstock in step a) to a temperature within a range of from 315° C. to 705° C.


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