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公开(公告)号:US20170341016A1
公开(公告)日:2017-11-30
申请号:US15676149
申请日:2017-08-14
Applicant: General Electric Company
Inventor: Irina Pavlovna SPIRY , Benjamin Rue WOOD , Surinder Prabhjot SINGH , Robert James PERRY , John Brian MCDERMOTT
CPC classification number: B01D53/1475 , B01D53/1425 , B01D53/62 , B01D53/96 , B01D2252/2026 , B01D2252/20489 , B01D2252/2053 , B01D2257/504 , B01D2258/0283 , Y02C10/06
Abstract: A method for treatment of a flue gas involves feeding the flue gas and a lean solvent to an absorber. The method further involves reacting the flue gas with the lean solvent within the absorber to generate a clean flue gas and a rich solvent. The method also involves feeding the clean flue gas from the absorber and water from a source, to a wash tower to separate a stripped portion of the lean solvent from the clean flue gas to generate a washed clean flue gas and a mixture of the water and the stripped portion of the lean solvent. The method further involves treating at least a portion of the mixture of the water and the stripped portion of the lean solvent via a separation system to separate the water from the stripped portion of the lean solvent.
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公开(公告)号:US20170158717A1
公开(公告)日:2017-06-08
申请号:US14962199
申请日:2015-12-08
Applicant: GENERAL ELECTRIC COMPANY
Inventor: Irina Pavlovna SPIRY , Robert James PERRY , Benjamin Rue WOOD , Surinder Prabhjot SINGH , Rachel Lizabeth FARNUM , Sarah Elizabeth GENOVESE
CPC classification number: C07F7/20 , B01D5/0036 , B01D5/009 , B01D53/002 , B01D53/1425 , B01D53/1475 , B01D53/18 , B01D2252/204 , B01D2256/22 , B01D2257/704 , B01D2257/80 , Y02P70/34
Abstract: The present invention is directed to aminosilicone solvent recovery methods and systems. The methods and systems disclosed herein may be used to recover aminosilicone solvent from a carbon dioxide containing vapor stream, for example, a vapor stream that leaves an aminosilicone solvent desorber apparatus. The methods and systems of the invention utilize a first condensation process at a temperature from about 80° C. to about 150° C. and a second condensation process at a temperature from about 5° C. to about 75° C. The first condensation process yields recovered aminosilicone solvent. The second condensation process yields water.
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