IP Library Granted Patent US 9,819,038
Granted Patent B2
US 9,819,038 · App. 13/907,647 · Granted Nov 14, 2017

Fuel cell reforming system with carbon dioxide removal

Inventors: Andrew Philip Shapiro (Schenectady, NY); Robert James Perry (Niskayuna, NY); Matthew Joseph Alinger (Delmar, NY); Bruce Philip Biederman (Old Greenwich, CT); Irfan Saif Hussaini (Glenville, NY); Irina Spiry (Gloversville, NY)
Assignee: General Electric Company
H01M8/0668H01M8/04007H01M8/0612H01M8/0662H01M2008/1293H01M2250/40H01M2250/402H01M2250/407Y02B90/12Y02E60/56Y02E60/563Y02P90/40
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Quick Facts
Patent No.
US 9,819,038
App. No.
13/907,647
Granted
Nov 14, 2017
Kind
B2
Abstract

A power generation system includes a fuel cell including an anode that generates a tail gas. The system also includes a hydrocarbon fuel reforming system that mixes a hydrocarbon fuel with the fuel cell tail gas and to convert the hydrocarbon fuel and fuel tail gas into a reformed fuel stream including CO 2 . The reforming system further splits the reformed fuel stream into a first portion and a second portion. The system further includes a CO 2 removal system coupled in flow communication with the reforming system. The system also includes a first reformed fuel path coupled to the reforming system. The first path channels the first portion of the reformed fuel stream to an anode inlet. The system further includes a second reformed fuel path coupled to the reforming system. The second path channels the second portion of the reformed fuel stream to the CO 2 removal system.

Claims (18)

1. A method of generating electric power with a power generation system utilizing a fuel cell, said method comprising:

channeling a fuel to an inlet of a solid oxide fuel cell anode;

generating a tail gas stream including carbon dioxide (CO 2 ) in the solid oxide fuel cell anode and discharging the tail gas stream from an outlet of the fuel cell anode;

channeling the tail gas stream to a hydrocarbon fuel reforming system;

mixing a hydrocarbon fuel with the tail gas stream to form a fuel/tail gas mixture stream;

at least partially converting the fuel/tail gas mixture stream into a reformed fuel stream including CO 2 ;

splitting the reformed fuel stream including CO 2 into a first portion and a second portion, wherein the first portion includes a hot partially reformed fuel stream;

channeling the first portion of the reformed fuel stream including CO 2 to the inlet of the solid oxide fuel cell anode;

channeling the second portion of the reformed fuel stream to a CO 2 removal system;

wherein channeling the second portion of the reformed fuel stream including CO 2 to a CO 2 removal system comprises decreasing a CO 2 concentration in the first portion of the reformed fuel stream including CO 2 comprising:

channeling the second portion of the reformed fuel stream including CO 2 to a solvent-based CO 2 absorber;

transferring at least a portion of the CO 2 in the second portion of the reformed fuel stream including CO 2 to a CO 2 -lean solvent stream, and

forming a CO 2 -rich solvent stream and a reformed fuel stream without CO 2 ; and channeling the reformed fuel stream without CO 2 into the hot partially reformed fuel stream.

2. The method in accordance with claim 1 , wherein decreasing a CO 2 concentration in the first portion of the reformed fuel stream including CO 2 further comprises: channeling the CO 2 -rich solvent stream to a rich solvent reboiler; adding heat into the rich solvent reboiler from at least one of a combustion engine exhaust stream and a heat pump.

3. The method in accordance with claim 2 , wherein adding heat into the rich solvent reboiler from at least one of a combustion engine exhaust stream and a heat pump comprises:

splitting the reformed fuel stream including CO 2 into a third portion; and

channeling the third portion of the reformed fuel stream including CO 2 to a combustion engine and generating the engine exhaust stream.

4. The method in accordance with claim 1 , wherein decreasing a CO 2 concentration in the first portion of the reformed fuel stream including CO 2 further comprises transferring heat from the CO 2 -lean solvent stream to the CO 2 -rich solvent stream through a solvent recuperator, thereby preheating the CO 2 -rich solvent stream prior to entry into the rich solvent reboiler.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 4, 2025
From: CUMMINS ENTERPRISE LLC
To: GE VERNOVA INFRASTRUCTURE TECHNOLOGY LLC
Reel/Frame 071849/0550 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 28, 2023
From: GENERAL ELECTRIC COMPANY
To: CUMMINS ENTERPRISE LLC
Reel/Frame 063486/0408 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 31, 2013
From: SHAPIRO, ANDREW PHILIP; PERRY, ROBERT JAMES; ALINGER, MATTHEW JOSEPH; BIEDERMAN, BRUCE PHILIP; HUSSAINI, IRFAN SAIF; SPIRY, IRINA
To: GENERAL ELECTRIC COMPANY
Reel/Frame 030527/0971 →
Continuity (2)
Continuation In Part 13077066 · Mar 31, 2011
Related Publication 20130260268A1 · Oct 3, 2013