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:
Dec. 30, 2003

Filed:

Jul. 31, 2001
Applicant:
Inventor:

Richard K. Lyon, Pittstown, NJ (US);

Assignee:

General Electric Co., Schenectady, NY (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 3/120 ; C01B 3/02 ;
U.S. Cl.
CPC ...
C01B 3/120 ; C01B 3/02 ;
Abstract

A process for burning coal to produce substantially pure hydrogen for use in fuel cells, together with “sequestration ready” carbon dioxide and a stream of oxygen depleted air for powering gas turbines, characterized by using a combination of two fluidized bed reactors and a third transfer line reactor, the first reactor being supplied with coal particles or “char” and fluidized with high temperature steam; the second reactor being fluidized with high temperature steam and the third reactor being fluidized by compressed air. Solids circulated among these three reactors include a mixture of materials containing calcium compounds (present as CaO, CaCO and mixtures thereof) and iron compounds (present as FeO, Fe O and mixtures thereof). The coal is gasified by the steam in the presence of CaO to produce CaCO and relatively pure hydrogen for use in fuel cells per a CO acceptor process. Because only part of the coal char input to the first reactor is gasified to produce hydrogen, the remainder can be burned to supply thermal energy necessary to regenerate the CaCO back to CaO. Carbon in the middle bed fluidized bed reactor reacts with Fe O in the third reactor and the temperature in the middle fluidized bed reactor is sufficiently high to decompose CaCO back into CaO.


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