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.
Patent No.:
Date of Patent:
Jul. 22, 2014
Filed:
Nov. 20, 2009
Sanjay K. Dube, Knoxville, TN (US);
Rameshawar S. Hiwale, Knoxville, TN (US);
Peter U. Koss, Zollikon, CH;
David J. Muraskin, Knoxville, TN (US);
Sanjay K. Dube, Knoxville, TN (US);
Rameshawar S. Hiwale, Knoxville, TN (US);
Peter U. Koss, Zollikon, CH;
David J. Muraskin, Knoxville, TN (US);
ALSTOM Technology Ltd, Baden, CH;
Abstract
A system for removing carbon dioxide from a flue gas stream is provided, the system comprising an absorber vessel configured to receive a flue gas stream, the absorber vessel comprising a first absorption stage configured to receive the flue gas stream and contact it with a first ionic solution, a second absorption stage configured to receive flue gas which has passed the first absorption stage and contact it with a second ionic solution, a first sump vessel, and a second sump vessel. Furthermore, a method for removing COfrom a flue gas stream containing COis provided, the method comprising the steps of a) contacting a flow of a first ionic solution comprising NHwith a flue gas stream to remove a first portion of COfrom the flue gas stream, b) collecting the used ionic solution from step a) in a first sump vessel, c) recycling ionic solution from the first sump vessel to step a), d) contacting a flow of a second ionic solution comprising NHwith the flue gas stream to remove a second portion of COfrom the flue gas stream, e) collecting the used ionic solution from step d) in a second sump vessel, and f) recycling ionic solution from the second sump vessel to step d).