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:
Nov. 10, 2015

Filed:

Jul. 08, 2013
Applicant:

The Southern Company, Birmingham, AL (US);

Inventors:

Guohai Liu, Birmingham, AL (US);

Pannalal Vimalchand, Birmingham, AL (US);

WanWang Peng, Birmingham, AL (US);

Assignee:

SOUTHERN COMPANY, Birmingham, AL (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10J 3/56 (2006.01); C10J 3/84 (2006.01); C10J 3/72 (2006.01); C10K 1/02 (2006.01); C10K 3/00 (2006.01);
U.S. Cl.
CPC ...
C10J 3/56 (2013.01); C10J 3/721 (2013.01); C10J 3/84 (2013.01); C10K 1/024 (2013.01); C10K 1/026 (2013.01); C10K 3/005 (2013.01); C10J 2300/093 (2013.01); C10J 2300/094 (2013.01); C10J 2300/0976 (2013.01); C10J 2300/1838 (2013.01); C10J 2300/1846 (2013.01); C10J 2300/1884 (2013.01); C10J 2300/1892 (2013.01);
Abstract

This invention relates to gasification of high ash bituminous coals that have high ash fusion temperatures. The ash content can be in 15 to 45 weight percent range and ash fusion temperatures can be in 1150° C. to 1500° C. range as well as in excess of 1500° C. In a preferred embodiment, such coals are dealt with a two stage gasification process—a relatively low temperature primary gasification step in a circulating fluidized bed transport gasifier followed by a high temperature partial oxidation step of residual char carbon and small quantities of tar. The system to process such coals further includes an internally circulating fluidized bed to effectively cool the high temperature syngas with the aid of an inert media and without the syngas contacting the heat transfer surfaces. A cyclone downstream of the syngas cooler, operating at relatively low temperatures, effectively reduces loading to a dust filtration unit. Nearly dust- and tar-free syngas for chemicals production or power generation and with over 90%, and preferably over about 98%, overall carbon conversion can be achieved with the preferred process, apparatus and methods outlined in this invention.


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