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. 06, 2016

Filed:

Mar. 30, 2011
Applicants:

Saravanan Subramani, Faridabad, IN;

Debasis Bhattacharyya, Faridabad, IN;

Reshmi Manna, Faridabad, IN;

Satyen Kumar Das, Faridabad, IN;

Tridib Sarkar, Faridabad, IN;

Santanam Rajagopal, Faridabad, IN;

Inventors:

Saravanan Subramani, Faridabad, IN;

Debasis Bhattacharyya, Faridabad, IN;

Reshmi Manna, Faridabad, IN;

Satyen Kumar Das, Faridabad, IN;

Tridib Sarkar, Faridabad, IN;

Santanam Rajagopal, Faridabad, IN;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 51/04 (2006.01); B01J 8/28 (2006.01); B01J 8/00 (2006.01); B01J 8/18 (2006.01); C10G 11/18 (2006.01); C10G 51/06 (2006.01);
U.S. Cl.
CPC ...
B01J 8/28 (2013.01); B01J 8/0055 (2013.01); B01J 8/1863 (2013.01); C10G 11/182 (2013.01); C10G 11/185 (2013.01); C10G 51/06 (2013.01); B01J 2208/00752 (2013.01); B01J 2208/00911 (2013.01); C10G 2300/104 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1059 (2013.01); C10G 2300/1074 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4018 (2013.01); C10G 2300/4025 (2013.01); C10G 2300/4093 (2013.01); C10G 2300/703 (2013.01); C10G 2300/708 (2013.01); C10G 2300/807 (2013.01); C10G 2400/02 (2013.01); C10G 2400/20 (2013.01); C10G 2400/28 (2013.01); C10G 2400/30 (2013.01);
Abstract

The invention provides for a process and apparatus for simultaneous conversion of lighter and heavier hydrocarbon feedstocks into improved yields of light olefins in the range of C2 to C4, liquid aromatics in the range C6 to C8 mainly benzene, toluene, xylene and ethyl benzene and other useful products employing at least two different reactors operated in series with respect to catalyst flow and parallel with respect to feed flow under different regimes and process conditions with same catalyst system.


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