Enhanced electrochemical oxidation of carbonaceous deposits in liquid-hydrocarbon fueled solid oxide fuel cells

Patent metadata

Field	Value
Publication number	US-10056635-B2
Application number	US-201514623884-A
Country	US
Kind code	B2
Filing date	Feb 17, 2015
Priority date	Feb 17, 2015
Publication date	Aug 21, 2018
Grant date	Aug 21, 2018

Abstract

Embodiments of a method of removing carbonaceous deposits in a liquid-hydrocarbon fueled solid oxide fuel cell and related system are provided. The method includes providing a solid oxide fuel cell system having an anode, a cathode, a solid oxide electrolyte oriented between the anode and cathode, an amplifier cathode disposed proximate the solid oxide electrolyte and the cathode, a fuel cell electric circuit electrically connecting the anode and the cathode, and an amplifier electric circuit electrically connecting the anode and the amplifier cathode. Further, operating the amplifier electric circuit in an electrolytic mode to electrically power the amplifier cathode, wherein the amplifier cathode generates and supplies O 2− or CO 3 2− to the anode. The method further includes removing the carbonaceous deposits on the anode by converting the carbonaceous deposits to carbon dioxide gas via reaction with the O 2− or CO 3 2− and expelling the carbon dioxide gas.

First claim

What is claimed is:

1. A method of removing carbonaceous deposits in a liquid-hydrocarbon fueled solid oxide fuel cell, the method comprising:
providing a solid oxide fuel cell system comprising an anode, a cathode, a solid oxide electrolyte oriented between the anode and cathode, an amplifier cathode disposed proximate the solid oxide electrolyte and the cathode, a fuel cell electric circuit electrically connecting the anode and the cathode, and an amplifier electric circuit electrically connecting the anode and the amplifier cathode, wherein the amplifier electric circuit comprises at least one battery, potentiostat, or galvanostat that powers and controls the amplifier electric circuit;
operating the amplifier electric circuit in an electrolytic mode to electrically power the amplifier cathode, wherein the amplifier cathode generates and supplies O 2− or CO 3 2− to the anode; and
removing the carbonaceous deposits on the anode by converting the carbonaceous deposits to carbon dioxide gas via reaction with the O 2− or CO 3 2− and expelling the carbon dioxide gas.

2. The method of claim 1 , wherein the current supplied to the amplifier electric circuit is substantially constant over time.

3. The method of claim 2 , wherein the current supplied to the amplifier electric circuit maintains a voltage above the O 2 reduction potential and below the electrolyte reduction potential.

4. The method of claim 1 , wherein the current supplied to the amplifier electrode circuit is pulsed.

5. The method of claim 4 , wherein the solid oxide fuel cell system further comprises a control circuit to pulse the current supplied to the amplifier electrode circuit such that current is supplied when the power output of the solid oxide fuel cell system drops below 50% of initial operation without carbonaceous deposits.

6. The method of claim 1 , wherein the cathode and the amplifier cathode are different compositions.

7. The method of claim 1 , wherein the cathode, the amplifier cathode, or both is selected from the group consisting of at least one perovskite material of the general type ABO 3 or ABMO 3 or A 1-x Sr x Fe 1-y Co y O 3-δ or A 1-x B x M 1-y Mg y O 3-δ , wherein:
A is La, Sn, Nd, Gd, Ba or Dy,
B is a 2 + , 3 + , 4 + or 5 + cation, and
M is a transition metal.

8. The method of claim 7 , wherein the perovskite material is LaSrFeCoO 3-δ (LSCF), or LaSrMnO 3-δ (LSM), or Sr 2 MgMo 0.8 Nb 0.2 O 6-δ .

9. The method of claim 1 , wherein the anode comprises a metallic, metal oxide, or ceramic-metallic.

10. The method of claim 9 , wherein the anode comprises metal selected from the group consisting of iron (Fe), copper (Cu), nickel (Ni), cobalt (Co), molybdenum (Mo), gold (Au), ruthenium (Ru), rhodium (Rh), tungsten (W), chromium (Cr), terbium (Tb), magnesium (Mg), platinum (Pt), palladium (Pd), and combinations thereof.

11. The method of claim 1 , wherein the electrolyte is zirconia-based, ceria-based, titania-based, a perovskite oxide, or cationic carbonate-based.

12. The method of claim 1 , wherein the solid oxide fuel cell system further comprises a liquid fuel atomizer located to distribute the liquid-hydrocarbon fuel across the anode.

13. A method of removing carbonaceous deposits in a liquid-hydrocarbon fueled solid oxide fuel cell, the method comprising:
providing a solid oxide fuel cell system comprising an anode, a cathode, a solid oxide electrolyte oriented between the anode and cathode, an amplifier cathode disposed proximate the solid oxide electrolyte and the cathode, a fuel cell electric circuit electrically connecting the anode and the cathode, and an amplifier electric circuit comprising at least one battery, potentiostat, or galvanostat electrically connecting the anode and the amplifier cathode;
monitoring a power reaction speed of the solid oxide fuel cell system;
operating the amplifier electric circuit in an electrolytic mode to electrically power the amplifier cathode, wherein the amplifier cathode generates and supplies O 2− or CO 3 2− to the anode;
removing the carbonaceous deposits on the anode by converting the carbonaceous deposits to carbon dioxide gas via reaction with the O 2− or CO 3 2− and expelling the carbon dioxide gas; and
adjusting the current supplied to the amplifier electric circuit to obtain steady-state operation of the removal of the carbonaceous deposits on the anode.

14. The method of claim 13 , wherein the current supplied to the amplifier electric circuit is substantially constant over time.

15. The method of claim 13 , wherein the current supplied to the amplifier electrode circuit is pulsed.

16. The method of claim 13 , wherein the amplifier electric circuit further comprises at least one potentiostat that powers and controls the amplifier electric circuit.

17. The method of claim 13 , wherein the amplifier electric circuit further comprises at least one galvanostat that powers and controls the amplifier electric circuit.

18. The method of claim 11 , wherein the zirconia-based electrolytes are selected from the group consisting of yttria stabilized ZrO 2 (YSZ), scandia stabilized ZrO 2 (ScSZ), calcia stabilized ZrO 2 (CSZ), samaria stabilized ZrO 2 (SmSZ), and combinations thereof.

19. The method of claim 11 , wherein the ceria-based electrolytes are selected from the group consisting of gadolinium doped ceria (GDC), yttria doped ceria (YDC), samarium doped ceria (SmDC), scandium doped ceria (GDC), zirconium doped ceria (ZDC), gadolinia stabilized ceria (CGO) and combinations thereof.

Assignees

• Saudi Arabian Oil Co

Inventors

• Hammad Ahmad D
• Souentie Stamatios

Classifications

• H01M8/0656 Primary

  by electrochemical means (H01M8/065 takes precedence) · CPC title

• H01M8/1246

  the electrolyte consisting of oxides · CPC title

• H01M2008/1293

  Fuel cells with solid oxide electrolytes · CPC title

• H01M2300/0071

  Oxides · CPC title

• H01M8/12

  operating at high temperature, e.g. with stabilised ZrO2 electrolyte · CPC title