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:
Feb. 19, 2019

Filed:

Dec. 18, 2013
Applicant:

Reliance Industries Limited, Mumbai, IN;

Inventors:

Sateesh Daggupati, Khamman, IN;

Sukumar Mandal, Faridabad, IN;

Asit Kumar Das, Jamnagar, IN;

Ajit Vishwanath Sapre, Tampa, FL (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 23/04 (2006.01); B01J 27/25 (2006.01); B01J 27/232 (2006.01); C10J 3/46 (2006.01); B01J 29/08 (2006.01); B01J 29/40 (2006.01); B01J 37/02 (2006.01);
U.S. Cl.
CPC ...
C10J 3/466 (2013.01); B01J 23/04 (2013.01); B01J 27/232 (2013.01); B01J 27/25 (2013.01); B01J 29/084 (2013.01); B01J 29/40 (2013.01); B01J 37/0201 (2013.01); C10J 3/463 (2013.01); C10J 2300/0943 (2013.01); C10J 2300/0976 (2013.01); C10J 2300/0986 (2013.01); C10J 2300/1246 (2013.01); C10J 2300/1637 (2013.01); C10J 2300/1807 (2013.01); C10J 2300/1853 (2013.01); Y02P 20/52 (2015.11); Y02P 20/584 (2015.11);
Abstract

An improved process for the catalytic gasification of a carbonaceous feedstock in a dual fluidized bed reactor for producing synthesis gas is disclosed. The disclosure uses γ-alumina as a catalyst support i and heat carrier in the gasification zone (). The gasification zone () is operated at 700-750° C. to prevent substantial conversion of γ-alumina to α-alumina, which would manifest in the enablement of high catalyst loading and high recyclability. The catalyst is an alkali metal, preferably KCO, so that conversion proportional to total KCOto solid carbon ratio is achieved with as high KCOloading as 50 wt % on the solid support. The combustion zone () is operated at 800°-840° C., to prevent any conversion of the γ-alumina to α-alumina, so that catalyst recyclability of up to 98% is achieved between two successive cycles.


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