Aminosilicone solvent recovery methods and systems

Patent metadata

Field	Value
Publication number	US-9890183-B2
Application number	US-201514962199-A
Country	US
Kind code	B2
Filing date	Dec 8, 2015
Priority date	Dec 8, 2015
Publication date	Feb 13, 2018
Grant date	Feb 13, 2018

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.

First claim

What is claimed is:

1. A method for recovering aminosilicone solvent from a first gas stream, the method comprising:
performing an absorption process, wherein the absorption process comprises contacting a flue gas with a lean stream to form a clean flue gas stream and a rich stream;
performing a desorption process, wherein the desorption process comprises heat treating the rich stream at a temperature from about 120° C. to about 160° C. to form a lean stream and the first gas stream, wherein the rich stream comprises rich aminosilicone solvent, and wherein the lean stream comprises lean aminosilicone solvent;
performing a first condensation process, wherein the first condensation process comprises condensing the first gas stream at a temperature from about 80° C. to about 150° C. to form a recovered aminosilicone stream and a second gas stream, wherein the recovered aminosilicone stream comprises lean aminosilicone solvent and the second gas stream comprises carbon dioxide and water vapor; and
performing a second condensation process, wherein the second condensation process comprises condensing the second gas stream at a temperature from about 5° C. to about 75° C. to form a waste water stream and a third gas stream; wherein the waste water stream comprises water and the third gas stream comprises carbon dioxide.

2. The method of claim 1 , wherein the first gas stream and the recovered aminosilicone stream further comprise triethylene glycol.

3. The method of claim 1 , wherein the first gas stream further comprises rich aminosilicone solvent.

4. The method of claim 1 , wherein the recovered aminosilicone stream further comprises rich aminosilicone solvent.

5. The method of claim 1 , wherein the desorption process further comprises heat treating the recovered aminosilicone stream at a temperature from about 120° C. to about 160° C. to form the lean stream and, optionally, the first gas stream.

6. The method of claim 1 , further comprising:
performing a compression process on the third gas stream, wherein the compression process comprises compressing the third gas stream to form a compressed composition, wherein the compressed composition comprises high pressure carbon dioxide.

7. The method of claim 1 , wherein the first condensation process comprises condensing the first gas stream at a temperature from about 80° C. to about 110° C.

8. The method of claim 1 , wherein the first condensation process comprises condensing the first gas stream at a temperature from about 85° C. to about 95° C.

9. The method of claim 1 , wherein the second condensation process comprises condensing the second gas stream at a temperature from about 20° C. to about 70° C.

10. The method of claim 1 , wherein the second condensation process comprises condensing the second gas stream at a temperature from about 35° C. to about 45° C.

Assignees

• Gen Electric

Inventors

• Spiry Irina Pavlovna
• Perry Robert James
• Wood Benjamin Rue
• Singh Surinder Prabhjot
• Farnum Rachel Lizabeth
• Genovese Sarah Elizabeth

Classifications

• B01D53/002

  by condensation · CPC title

• B01D2252/204

  Amines · CPC title

• B01D53/18

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title

• B01D53/1425

  Regeneration of liquid absorbents · CPC title

• B01D53/1475

  Removing carbon dioxide · CPC title