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:
Sep. 26, 2017

Filed:

Jul. 04, 2011
Applicants:

Saidulu Gadari, Faridabad, IN;

Manoj Kumar Bhuyan, Faridabad, IN;

Hari Venkata Devi Prasad Terapalli, Faridabad, IN;

Debasis Bhattacharyya, Faridabad, IN;

Santanam Rajagopal, Faridabad, IN;

Inventors:

Saidulu Gadari, Faridabad, IN;

Manoj Kumar Bhuyan, Faridabad, IN;

Hari Venkata Devi Prasad Terapalli, Faridabad, IN;

Debasis Bhattacharyya, Faridabad, IN;

Santanam Rajagopal, Faridabad, IN;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 51/02 (2006.01); B01J 8/26 (2006.01); C10G 11/18 (2006.01); C10G 25/09 (2006.01); C10G 25/12 (2006.01); B01J 8/32 (2006.01); B01J 8/18 (2006.01); B01J 8/00 (2006.01); C10G 55/06 (2006.01); C10G 55/08 (2006.01); C10G 70/04 (2006.01); C10G 51/04 (2006.01);
U.S. Cl.
CPC ...
C10G 51/02 (2013.01); B01J 8/0055 (2013.01); B01J 8/1863 (2013.01); B01J 8/26 (2013.01); B01J 8/32 (2013.01); C10G 11/18 (2013.01); C10G 11/182 (2013.01); C10G 25/09 (2013.01); C10G 25/12 (2013.01); C10G 51/026 (2013.01); C10G 55/06 (2013.01); C10G 55/08 (2013.01); C10G 70/041 (2013.01); B01J 2208/0084 (2013.01); C10G 2300/205 (2013.01); C10G 2300/206 (2013.01); C10G 2300/305 (2013.01); C10G 2300/4081 (2013.01); C10G 2300/4093 (2013.01); C10G 2300/708 (2013.01); C10G 2300/807 (2013.01); C10G 2400/02 (2013.01); C10G 2400/20 (2013.01);
Abstract

This invention provides a fluidized catalytic cracking apparatus and process for converting a hydrocarbon feedstock containing higher concentrations of Conradson Carbon Residue (CCR), metal impurities, etc into lighter products by employing two riser reactors in which the feed impurities are removed using an adsorbent in a first riser reactor and cracking a portion of first riser reactor liquid product in a second riser reactor to lighter products using the active catalyst thus eliminating the catalyst deactivation due to metal, impurities and FCC catalyst activity dilution effect to achieve a better conversion and higher catalyst longevity.


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