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:
Jan. 24, 2017

Filed:

Aug. 14, 2014
Applicant:

Reliance Industries Limited, Mumbai, Maharashtra, IN;

Inventors:

Sukumar Mandal, Haryana, IN;

Manoj Yadav, Haryana, IN;

Amitkumar Parekh, Gujarat, IN;

Asit Kumar Das, Gujarat, IN;

Shubhangi Jaguste, Maharashtra, IN;

Praveen Kumar Chinthala, Andhra Pradesh, IN;

Gopal Ravichandran, Tamil Nadu, IN;

Mahesh Marve, Maharashtra, IN;

Ajit Sapre, Tampa, FL (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 4/06 (2006.01); C10G 11/18 (2006.01); B01J 29/08 (2006.01); B01J 29/40 (2006.01); B01J 29/80 (2006.01); B01J 29/90 (2006.01); B01J 38/30 (2006.01);
U.S. Cl.
CPC ...
C07C 4/06 (2013.01); C10G 11/18 (2013.01); C10G 11/182 (2013.01); C10G 11/185 (2013.01); B01J 29/084 (2013.01); B01J 29/40 (2013.01); B01J 29/80 (2013.01); B01J 29/90 (2013.01); B01J 38/30 (2013.01); C07C 2529/06 (2013.01); C07C 2529/40 (2013.01);
Abstract

A process for catalytic conversion of low value hydrocarbon streams to light olefins in comparatively higher yields is disclosed. Propylene is obtained in amounts higher than 20 wt. % and ethylene higher than 6 wt. %. The process is carried out in a preheated cracking reactor having a single riser and circulating an FCC catalyst. The riser is divided into three temperature zones in which different hydrocarbon feeds are introduced. An oxygenate feed is introduced in the operative top zone in the riser. Heat for the endothermic cracking is obtained by the exothermic reaction of converting the oxygenate feed into gas and/or from a regenerator in which the spent FCC catalyst is burnt.


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