SOFC including redox-tolerant anode electrode and system including the same

Patent metadata

Field	Value
Publication number	US-10680251-B2
Application number	US-201815915281-A
Country	US
Kind code	B2
Filing date	Mar 8, 2018
Priority date	Aug 28, 2017
Publication date	Jun 9, 2020
Grant date	Jun 9, 2020

Abstract

A solid oxide fuel cell, system including the same, and method of using the same, the fuel cell including an electrolyte disposed between an anode and a cathode. The anode includes a first layer including a metallic phase and a ceramic phase, and a second layer including a metallic phase. The metallic phase of the second layer includes a metal catalyst and a dopant selected from Al, Ca, Ce, Cr, Fe, Mg, Mn, Nb, Pr, Ti, V, W, or Zr, any oxide thereof, or any combination thereof. The second layer may also include a ceramic phase including ytterbia-ceria-scandia-stabilized zirconia (YCSSZ).

First claim

What is claimed is:

1. A solid oxide fuel cell (SOFC) comprising: an ionically conductive electrolyte;
an anode disposed on a first side of the electrolyte, the anode comprising: a first layer comprising a cermet comprising a ceramic phase and a metallic phase comprising a metal catalyst; and
a second layer comprising a metallic phase comprising a metal catalyst comprising NiO and a dopant comprising MgO; and
a cathode disposed on an opposing second side of the electrolyte,
wherein the first layer is disposed between the second layer and the electrolyte; and
wherein the metallic phase of the second layer comprises Mg x Ni 1-x O, wherein x ranges from about 0.01 to about 0.04.

2. The SOFC of claim 1 , wherein the metallic phase of the second layer comprises:
from about 1 to about 10 atomic percent of the dopant; and
from about 99 to about 90 atomic percent of the metal catalyst.

3. The SOFC of claim 1 , wherein the metallic phase of the second layer comprises:
from about 2 to about 4 atomic percent of the dopant; and
from about 98 to about 96 atomic percent of the metal catalyst.

4. The SOFC of claim 1 , wherein:
the first layer comprises from about 70 to about 90 wt % of the ceramic phase, and from about 10 to about 30 wt % of the metallic phase, based on the total weight of the first layer; and
the second layer comprises from about 15 to about 35 wt % of a ceramic phase, and from about 65 to about 85 wt % of the metallic phase, based on the total weight of the second layer.

5. The SOFC of claim 4 , wherein the metallic phase of the first layer further comprises a dopant selected from Al, Ca, Ce, Cr, Fe, Mg, Mn, Nb, Pr, Ti, V, W, or Zr, any oxide thereof, or any combination thereof.

6. The SOFC of claim 4 , wherein the ceramic phase of one or both of the first and second layers comprises ytterbia-ceria-scandia-stabilized zirconia (YCSSZ).

7. The SOFC of claim 4 , wherein the thickness of second layer ranges from about 5 μm to about 35 μm.

8. The SOFC of claim 4 , wherein:
the ceramic phase of the first layer comprises gadolinia-doped ceria (GDC), samaria-doped ceria (SDC), ytterbia-doped ceria (YDC), scandia-stabilized zirconia (SSZ), or a combination thereof;
the ceramic phase of the second layer comprises ytterbia-ceria-scandia-stabilized zirconia (YCSSZ);
the ceramic phases of both the first and second layers is free of yttria-stabilized zirconia (YSZ).

9. The SOFC of claim 8 , wherein the electrolyte comprises YCSSZ.

10. The SOFC of claim 4 , wherein the ceramic phases of both the first and second layers is free of yttria-stabilized zirconia (YSZ).

11. A method of operating a fuel cell system comprising a fuel cell stack comprising SOFC's of claim 1 , the method comprising:
operating the system in a power generation mode that comprises providing a fuel and an oxidant to the stack, to generate electricity; and
operating the system in a shutdown mode that comprises stopping the flow of the fuel and the oxidant to the stack, without intentionally providing an oxidizing purge gas to the stack before the stack reaches room temperature.

12. A solid oxide fuel cell (SOFC) comprising:
an ionically conductive electrolyte;
an anode disposed on a first side of the electrolyte, the anode comprising:
a first layer comprising a cermet comprising a ceramic phase and a metallic phase comprising a metal catalyst; and
a second layer comprising a cermet comprising a ceramic phase and a metallic phase comprising a metal catalyst; and
a cathode disposed on an opposing second side of the electrolyte,
wherein:
the first layer is disposed between the second layer and the electrolyte;
at least one of the first and the second layers further comprises a dopant selected from MgO or Mg;
the dopant is located in the second layer and comprises MgO;
the metal catalyst of the second layer comprises NiO; and
the metallic phase of the second layer comprises Mg x Ni 1-x O, wherein x ranges from about 0.01 to about 0.04.

13. The SOFC of claim 12 , wherein:
the first layer comprises from about 70 to about 90 wt % of the ceramic phase, and from about 10 to about 30 wt % of the metallic phase, based on the total weight of the first layer; and
the second layer comprises from about 15 to about 35 wt % of the ceramic phase, and from about 65 to about 85 wt % of the metallic phase, based on the total weight of the second layer.

14. The SOFC of claim 13 , wherein:
the ceramic phase of the first and the second layer comprises samaria doped ceria;
the thickness of the second layer ranges from about 10 μm to about 25 μm; and
after thirteen redox cycles, the SOFC has a voltage loss of less than about 600 mV.

15. A solid oxide fuel cell (SOFC) comprising:
an ionically conductive electrolyte;
an anode disposed on a first side of the electrolyte, the anode comprising:
a first layer comprising a cermet comprising a ceramic phase and a metallic phase comprising a metal catalyst; and
a second layer comprising a metallic phase comprising a metal catalyst and a dopant selected from Al, Ca, Ce, Cr, Fe, Mg, Mn, Nb, Pr, Ti, V, W, or Zr, any oxide thereof, or any combination thereof; and
a cathode disposed on an opposing second side of the electrolyte,
wherein the first layer is disposed between the second layer and the electrolyte; and
wherein the metallic phase of the second layer comprises:
from about 2 to about 4 atomic percent of the dopant; and
from about 98 to about 96 atomic percent of the metal catalyst.

Assignees

• Bloom Energy Corp

Inventors

• Gasda Michael
• El Batawi Emad
• Armstrong Tad
• RADHAKRISHNAN Vijay
• Scholl Jonathan

Classifications

• H01M4/8657 Primary

  layered · CPC title

• H01M4/905

  specially used in fuel cell operating at high temperature, e.g. SOFC · CPC title

• H01M2008/1293

  Fuel cells with solid oxide electrolytes · CPC title

• H01M4/9066

  of metal-ceramic composites or mixtures, e.g. cermets · CPC title

• H01M2004/8684

  Negative electrodes · CPC title