IP Library Granted Patent US 9,764,274
Granted Patent B2
US 9,764,274 · App. 14/567,319 · Granted Sep 19, 2017

System and method for treatment of a flue gas

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Quick Facts
Patent No.
US 9,764,274
App. No.
14/567,319
Granted
Sep 19, 2017
Kind
B2
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.

Claims (11)

1. A system for treatment of a flue gas, the system comprising:

an absorber for receiving a flue gas and configured to react the flue gas with a lean solvent to generate a clean flue gas and a rich solvent;

a wash tower coupled to the absorber and a source, for receiving the clean flue gas and water respectively and configured 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; and

a separation system comprising a splitter coupled to the wash tower and a decanter coupled to the splitter, wherein the splitter is configured to separate at least a portion of the mixture of the water and the stripped portion of the lean solvent, and wherein the decanter is configured to separate a water phase portion from a solvent phase portion of at least the portion of the mixture of the water and the stripped portion of the lean solvent.

2. The system of claim 1 , wherein the lean solvent comprises aminosilicone.

3. The system of claim 1 , wherein the absorber is further configured to remove carbon dioxide from the flue gas, using the lean solvent.

4. The system of claim 1 , wherein the separation system further comprises a distillation device coupled to the decanter via a bypass path and configured to separate at least a portion of the water from the water phase portion to generate a solvent portion.

5. The system of claim 1 , further comprising a treatment device coupled to the absorber and configured to receive the rich solvent and treat the rich solvent to separate carbon dioxide from the rich solvent.

6. The system of claim 1 , wherein the separation system further comprises a membrane separator coupled to the decanter and configured to separate at least a first portion of the water from the water phase portion to generate a first solvent portion.

7. The system of claim 6 , wherein the separation system further comprises a distillation device coupled to the membrane separator and configured to separate a second portion of the water from the first solvent portion to generate a second solvent portion.

8. The system of claim 7 , wherein the system is configured to recirculate the second solvent portion to the absorber.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 26, 2020
From: GENERAL ELECTRIC COMPANY
To: BAKER HUGHES, A GE COMPANY, LLC
Reel/Frame 051699/0052 →
CONFIRMATORY LICENSE Recorded Mar 7, 2018
From: GENERAL ELECTRIC GLOBAL RESEARCH CTR
To: UNITED STATES DEPARTMENT OF ENERGY
Reel/Frame 045518/0604 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 9, 2015
From: SPIRY, IRINA PAVIOVNA; WOOD, BENJAMIN RUE; SINGH, SURINDER PRABHJOT; PERRY, ROBERT JAMES; MCDERMOTT, JOHN BRIAN
To: GENERAL ELECTRIC COMPANY
Reel/Frame 034670/0418 →