IP Library Granted Patent US 7,521,139
Granted Patent B2
US 7,521,139 · App. 10/502,957 · Granted Apr 21, 2009

Thermal management of fuel cells

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Quick Facts
Patent No.
US 7,521,139
App. No.
10/502,957
Granted
Apr 21, 2009
Kind
B2
Abstract

A method for the thermal management of a fuel cell, which method comprises: processing a fuel supply stream in an autothermal reformer to produce a fuel cell supply stream comprising a concentration of methane; and reforming within the fuel cell methane present in the fuel cell supply stream, wherein the concentration of methane in the fuel cell supply stream is controlled by operation of the autothermal reformer in order to achieve a desired level of reforming of methane within the fuel cell.

Claims (15)

1. A method for the thermal management of a fuel cell, which method comprises: processing a fuel supply stream in an autothermal reformer to produce a fuel cell supply stream comprising a concentration of methane; and reforming within the fuel cell methane present in the fuel cell supply stream, wherein the concentration of methane in the fuel cell supply stream is controlled by operation of the autothermal reformer in order to achieve a desired level of reforming of methane within the fuel cell.

2. A method according to claim 1 , wherein the methane concentration in the output stream of the autothermal reformer may be varied on a continuous and rapid basis thereby allowing the extent of internal reforming of methane within the fuel cell to be controlled in response to fluctuations in fuel cell temperature.

3. A method according to claim 1 , wherein the fuel supply stream is natural gas, LPG or diesel.

4. A method according to claim 1 , wherein the autothermal reformer combines catalytic partial oxidation and steam reforming reactions.

5. A method according to claim 4 , wherein the concentration of methane in the fuel cell supply stream is controlled by controlling the temperature of the reformer aspect of the autothermal reformer.

6. A method according to claim 4 , wherein the extent of catalytic partial oxidation is controlled by adjusting the amount of oxygen available for the reaction.

7. A method according to claim 4 , wherein the extent of steam reforming in the autothermal reformer is adjusted by controlling the amount of water available for reaction.

8. A method according to claim 1 , wherein the methane concentration in the output of the autothermal reformer is controlled by adjusting the temperature and/or pressure at which the autothermal reformer is operated.

9. A method according to claim 1 , wherein the autothermal reformer is provided with a series of catalyst-coated and uncoated channels configured in such a way that the fuel supply stream may be caused to flow through selected channels based upon the required degree of contact between the fuel supply stream and catalyst in the autothermal reformer, thereby controlling the methane concentration in the fuel cell feed stream.

10. A method according to claim 1 , wherein the autothermal reformer includes a catalyst whose activity varies with the oxygen to carbon ratio in the fuel supply stream.

11. A method according to claim 1 , wherein the methane concentration of the fuel cell supply stream is at least 10% by volume.

12. A fuel cell system which allows thermal management of a fuel cell, comprising:

an autothermal reformer configured to produce an output stream having controlled methane concentration provided upstream of and in communication with a fuel cell;

a fuel cell configured to internally reform methane provided downstream of and in communication with the autothermal reform; and

a control unit configured to measure a temperature of said fuel cell and to vary the operation of the autothermal reformer in order to control concentration of the methane in an output stream of the autothermal reformer during operation of the autothermal reformer so that the internal reforming of the methane within the fuel cell takes place at an appropriate level to control the temperature of the fuel cell.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 10, 2016
From: CNPC XING DE ENERGY SHARE LIMITED
To: CHAOZHOU THREE-CIRCLE (GROUP) CO., LTD.
Reel/Frame 037753/0632 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE'S ADDRESS PREVIOUSLY RECORDED ON REEL 036920 FRAME 0234. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Nov 2, 2015
From: CERAMIC FUEL CELLS LIMITED
To: CNPC XING DE ENERGY SHARE LIMITED
Reel/Frame 037150/0400 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 30, 2015
From: CERAMIC FUEL CELLS LIMITED
To: CNPC XING DE ENERGY SHARE LIMITED
Reel/Frame 036920/0234 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 28, 2004
From: FOGER KARL
To: CERAMIC FUEL CELLS LIMITED
Reel/Frame 015935/0665 →