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:
Oct. 28, 2014

Filed:

Oct. 16, 2013
Applicant:

Alstom Technology Ltd, Baden, CH;

Inventors:

Olaf Stallmann, Essenheim, DE;

Gerhard Heinz, Esslingen, DE;

Peter Ulrich Koss, Baden, CH;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/50 (2006.01); B01D 53/62 (2006.01); B01D 53/74 (2006.01); B01D 53/75 (2006.01); F23J 15/02 (2006.01); B01D 53/83 (2006.01); B01D 53/34 (2006.01);
U.S. Cl.
CPC ...
F23J 15/022 (2013.01); B01D 53/83 (2013.01); B01D 2251/404 (2013.01); Y02C 10/06 (2013.01); B01D 53/75 (2013.01); B01D 2251/602 (2013.01); B01D 53/343 (2013.01); B01D 53/508 (2013.01); Y02C 10/04 (2013.01); B01D 2258/0283 (2013.01); F23J 15/02 (2013.01); B01D 53/62 (2013.01); B01D 2251/606 (2013.01);
Abstract

A method for combustion of a fuel and treatment of the resulting flue gas includes: combusting a fuel to produce a hot flue gas stream containing at least carbon dioxide (CO) and sulfur dioxide (SO), bringing the flue gas stream into contact with solid calcium oxide (CaO) in a carbonation reactor operating at a temperature at which COin the flue gas reacts with CaO to form solid calcium carbonate (CaCO), heating CaCOin a calcination reactor operating at a temperature at which CaCOis converted to CaO and CO, and recirculating CaO formed in the calcination reactor back to the carbonation reactor. Heating can be at least partially effected by indirect heat exchange with hot flue gas from the combustion. Flue gas used for the indirect heat exchange can be subsequently subjected to dry desulfurization before it is brought into contact with CaO in the carbonation reactor.


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