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:
Jun. 10, 2008

Filed:

Jun. 14, 2006
Applicants:

Keith Holroyd Kuechler, Friendswood, TX (US);

James R. Lattner, Seabrook, TX (US);

Nicolas P. Coute, Houston, TX (US);

Jeffrey S. Smith, Seabrook, TX (US);

Justin Leonard Krieger, Alexandria, VA (US);

Inventors:

Keith Holroyd Kuechler, Friendswood, TX (US);

James R. Lattner, Seabrook, TX (US);

Nicolas P. Coute, Houston, TX (US);

Jeffrey S. Smith, Seabrook, TX (US);

Justin Leonard Krieger, Alexandria, VA (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 1/00 (2006.01);
U.S. Cl.
CPC ...
Abstract

The present invention is directed to a hydrocarbon conversion apparatus and process. The apparatus comprises the following: a plurality of riser reactors, each having a first end into which a catalyst is fed, a second end through which the catalyst can exit, and optionally a center axis extending therebetween. The apparatus also includes a separation zone having a plurality of inlets, each inlet not being oriented along the center axes of the riser reactors, the separation zone being provided to separate the catalyst from products of a reaction conducted in the hydrocarbon conversion apparatus. A plurality of deviating members are also provided, each deviating member being in fluid communication between the second end of a respective riser reactor and a respective inlet of the separation zone. The apparatus also includes a catalyst retention zone provided to contain catalyst, which is fed to the riser reactors. A catalyst return is in fluid communication between the separation zone and the catalyst retention zone.


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