WO2017205660A1 - Electrode comprising heavily-doped ceria - Google Patents

Electrode comprising heavily-doped ceria Download PDF

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Publication number
WO2017205660A1
WO2017205660A1 PCT/US2017/034534 US2017034534W WO2017205660A1 WO 2017205660 A1 WO2017205660 A1 WO 2017205660A1 US 2017034534 W US2017034534 W US 2017034534W WO 2017205660 A1 WO2017205660 A1 WO 2017205660A1
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WO
WIPO (PCT)
Prior art keywords
ceria
vol
electrode
phase
functional layer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US2017/034534
Other languages
French (fr)
Inventor
Sophie Marie Claire POIZEAU
Deniz Cetin
Srikanth Gopalan
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Boston University
Saint Gobain Ceramics and Plastics Inc
Original Assignee
Boston University
Saint Gobain Ceramics and Plastics Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Boston University, Saint Gobain Ceramics and Plastics Inc filed Critical Boston University
Priority to DK17803610.9T priority Critical patent/DK3465807T3/en
Priority to KR1020187036566A priority patent/KR102185472B1/en
Priority to CN201780042762.XA priority patent/CN109690847B/en
Priority to JP2018561690A priority patent/JP6740528B2/en
Priority to EP17803610.9A priority patent/EP3465807B1/en
Priority to KR1020207033352A priority patent/KR102248541B1/en
Publication of WO2017205660A1 publication Critical patent/WO2017205660A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the present disclosure relates to electrodes and devices comprising the electrodes.
  • operating temperatures greater than 700°C are desirable for the more facile kinetics of the gas reactants and lower resistance of the ionic membrane.
  • High operating temperatures also allow internal reformation of hydrocarbon fuels, which can reduce the system size significantly compared to systems with external reforming.
  • the high operating temperatures can reduce electrode performance. A need exists for an improved electrode material.
  • FIGs.1 to 8 include graphs of XRD patterns for various Samples described in the Examples.
  • FIG.9 includes a photograph of an SOFC button cell described in the Examples.
  • FIG.10 includes a graph of performance characteristics of the SOFC button cell of FIG.9.
  • the term“vol%,” when used herein to describe the composition of a layer, refers to a percentage of the total volume of the solids, e.g., excluding porosity, of the layer.
  • the term“mol%,” when used herein to describe a dopant concentration refers to a percentage of the total amount, in moles, of cations in a given compound.
  • the oxygen stoichiometry in any of the formulas provided below may vary slightly and, thus, is considered to include a delta (excess or deficiency), referred to as“d”, of +/- 0.5.
  • a doped ceria can have oxygen understoichiometry (oxygen deficiency) where d is a deficiency of at most 0.29, at most 0.27, or at most 0.25; and an Ln 2 MO 4+d can have oxygen overstoichiometry (oxygen excess) where d is an excess of at most 0.34, at most 0.32, or at most 0.3.
  • La 0.40 Ce 0.60 O 2 would include, e.g., La 0.40 Ce 0.60 O 2-d , where d is at at most 0.25
  • La 2 NiO 4+d would include, e.g., La 2 NiO 4+d , where d is at most 0.3.
  • An electrode can include a composite functional layer including a heavily-doped ceria that is suitable for operating temperatures of greater than 700°C.
  • the term “heavily-doped” refers to a dopant concentration of at least 40 mol%.
  • the electrode can include a first phase comprising the heavily-doped ceria and a second phase including an Ln 2 MO 4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal, without the reactivity problems encountered with existing composite electrode materials.
  • High temperature electrochemical cells can include a number of requirements for high performance.
  • the materials should withstand processing temperatures of at least 1000°C without decomposing or forming resistive phases and maintain a stable composition and crystal structure at operating conditions.
  • the functional layers should retain porosity and facile electron transfer reaction kinetics.
  • Ln 2 MO 4 materials can generally provide high electrode performance, where Ln is any of the lanthanide elements and M is a 3d transition metal.
  • the Ln 2 MO 4 family of materials can offer a wider operating temperature range (e.g., 700°C to 900°C) as compared to other materials only suitable for either higher or lower temperatures.
  • the Ln 2 MO 4 family of materials provides the additional advantage of mixed ionic electronic conductivity.
  • Ln 2 MO 4 family of materials can be reactive with common high temperature electrolytes.
  • Ln 2 MO 4 materials have a high coefficient of thermal expansion (referred to herein as“CTE”), reducing mechanical stability in a multilayer architecture.
  • CTE coefficient of thermal expansion
  • a rare earth-doped ceria can form a composite with the Ln 2 MO 4 materials to form a composite electrode with a reduced CTE.
  • a lightly-doped ceria can react with Ln 2 MO 4 when in intimate contact at elevated temperatures.
  • the term“lightly- doped” refers to a dopant concentration of less than 40 mol%.
  • the solubility limit is the amount of rare earth oxide that can be incorporated into the ceria lattice while maintaining its fluorite structure. Further, diffusional transport of the lanthanide element from the Ln 2 MO 4 into the ceria is suppressed since the dopant concentration is close to the solubility limit of Ln in ceria.
  • the Ln of the Ln 2 MO 4 phase includes at least one lanthanide.
  • the Ln of the Ln 2 MO 4 phase includes at least one lanthanide selected from the group consisting of La, Sm, Er, Pr, Nd, Gd, Dy, or any combination thereof.
  • the at least one lanthanide or combination thereof can be doped with a metal.
  • the metal dopant can include an alkaline earth metal.
  • the alkaline earth metal can include at least one alkaline earth selected from the group consisting of Sr, Ca, Ba, or any combination thereof to increase hole conductivity.
  • the M of the Ln 2 MO 4 phase includes a 3d transition metal.
  • the M of the Ln 2 MO 4 phase includes at least one 3d transition metal selected from the group consisting of Ni, Cu, Co, Fe, Mn or any combination thereof.
  • the heavily-doped ceria phase can include a ceria and at least one dopant such that the total dopant concentration is at least 40 mol% and no greater than the solubility limit of ceria.
  • the heavily-doped ceria can have the general formula:
  • Ce (1-x-y) A x B y O 2 where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
  • the rare earth dopant A includes at least one dopant selected from the group consisting of La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, or any combination thereof.
  • the rare earth dopant A includes at least one of La, Gd, Nd, or Sm.
  • x+y is at least 0.4, or greater than 0.4, or at least 0.41, or at least 0.42, or at least 0.43, or at least 0.44, or at least 0.45, or at least 0.46, or at least 0.47. It would be expected that the use of heavily-doped ceria for cathode functional layers would lead to lower ionic conductivity.
  • x+y is no greater than the solubility limit. In a particular embodiment, x+y is no greater than 0.5.
  • the alkaline earth dopant B includes at least one dopant selected from the group consisting of Sr, Ca, Ba, or any combination thereof.
  • y can be 0, meaning that the heavily-doped ceria phase does not include an alkaline earth dopant B. In other embodiments, y is at least 0.01, or at least 0.05, or at least 0.1. In other embodiments, y is at most 0.24, or at most 0.22, or at most 0.2.
  • a lightly-doped ceria phase can be reactive with an Ln 2 MO 4 phase.
  • Such a reaction can cause diffusion of the Ln into the lightly-doped ceria, leading to a reduction or even a complete removal of the Ln from the Ln 2 MO 4 phase.
  • such a reaction can lead to the presence of a metal oxide (MO) and/or a free rare earth oxide (RE 2 O 3 ), which were not initially present in the electrode, particularly when M is Ni.
  • the reactivity is reduced or avoided such that, in an embodiment, less than 5 vol% of free RE 2 O 3 rare earth oxide is detectable in the functional layer of the electrode. In an embodiment, less than 5 vol% of MO metal oxide is detectable in the functional layer of the electrode.
  • the detection method is x-ray diffraction having a detection limit of 5 vol%.
  • the ceria phase can be present in the functional layer of the electrode in an amount of at least 40 vol%, or at least 45 vol%, or at least 50 vol%, or at least 55 vol%, or at least 60 vol%, or at least 65 vol%, or at least 70 vol%, or at least 75 vol%, based on a total volume of the functional layer minus the volume occupied by porosity.
  • a lightly-doped ceria phase increasing the volume percent of the ceria phase would increase the likelihood of rare earth diffusion.
  • higher performance for composite electrodes including a lightly-doped ceria phase would be exhibited at lower concentrations of the ceria phase.
  • the thermodynamic stability is increased and, thus, the volume percent of the ceria phase can be increased without increasing the likelihood of rare earth diffusion.
  • the functional layer of the electrode has a porosity of at least 10 vol%, or at least 15 vol%, or at least 18 vol%, based on a total volume of the functional layer. Further, in an embodiment, the functional layer of the electrode has a porosity of at most 60 vol%, or at most 50 vol%, or at most 40 vol%, or at most 35 vol%, based on a total volume of the functional layer. The porosity is determined by image analysis of the cross section of the layer using an image analysis tool such as ImageJ to view and measure the porosity by contrast.
  • the functional layer of the electrode has the functional layer has a thickness of at least 5 micron, or at least 10 microns, or at least 12 microns, or at least 15 microns, or at least 20 microns. Further, in an embodiment, the functional layer of the electrode has a thickness of at most 100 microns, at most 90 microns, at most 80 microns, or at most 70 microns.
  • the electrode described herein can be made by providing starter materials, mixing the starter materials, and sintering the mixture.
  • the starter materials include an Ln 2 MO 4 material, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal, and a ceria material comprising doped ceria having the general formula Ce (1-x-y) A x B y O 2 , where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
  • a binder system can be added to the material and the ceria material to form a slurry.
  • the binder system can include at least one polymer.
  • the slurry can be deposited by a ceramic forming technique such as spraying, tape casting or screen printing and then sintered to form an electrode having an Ln 2 MO 4 phase and a ceria phase.
  • the sintering temperature can be greater than the operating temperature.
  • the sintering temperature can be at least 1000°C, or at least 1100°C, or at least 1200°C, or at least 1300°C.
  • the sintering temperature can be no greater than 1800°C, or no greater than 1700°C, or no greater than 1600°C.
  • the electrode described herein can be utilized as a component in a variety of devices including electrochemical devices, sensor devices, and the like.
  • the electrochemical device including the electrode described herein comprises an electrolyte layer, an optional barrier layer, and an anode layer.
  • the electrolyte layer can comprise at least one electrolyte material selected from the group consisting of ceria, zirconia, lanthanum gallate, or a combination thereof.
  • the electrolyte material includes a stabilized zirconia.
  • the electrolyte layer includes a doped ceria having the general formula:
  • A is at least one rare earth dopant
  • B is at least one alkaline earth dopant
  • x is at least 0.05
  • y is in a range of 0 to 0.1
  • x+y is greater than 0.05 and less than 0.25.
  • A is La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, or any combination thereof.
  • B is Sr, Ca, Ba, or any combination thereof.
  • the electrolyte layer can have a thickness of at most 800 microns, or at most 600 microns, or at most 400 microns, or at most 200 microns, or at most 50 microns. Further, the electrolyte layer can have a thickness of at least 1 micron, at least 3 microns, or at least 5 microns.
  • the electrolyte layer can have a porosity of at most 10 vol%, or at most 8 vol%, or at most 6 vol%, or at most 4 vol%, based on a total volume of the electrolyte layer. Further, while the electrolyte may be completely dense, it is possible that some porosity can exist, such as at least 0.01 vol%, or at least 0.05 vol%, or at least 0.1 vol%.
  • the electrochemical device includes a barrier layer disposed between the electrode and the electrolyte layer.
  • the barrier layer includes doped ceria having the general formula:
  • A is at least one rare earth dopant
  • B is at least one alkaline earth dopant
  • x is at least 0.05
  • y is in a range of 0 to 0.2
  • x+y is greater than 0.05 and no greater than the solubility limit of ceria.
  • A is La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, Pr, or any combination thereof.
  • B is Sr, Ca, Ba, or any combination thereof.
  • the barrier layer has a porosity of at most 15 vol%, or at most 12 vol%, or at most 10 vol%, based on a total volume of the barrier layer. In an embodiment, the barrier layer has a porosity of at least 0.5 vol%, or at least 1 vol%, or at least 2 vol%, or at least 3 vol%, based on a total volume of the barrier layer.
  • the barrier layer has a thickness less than the electrolyte layer and the functional layer.
  • the electrochemical device includes a solid oxide fuel cell (also referred to as“SOFC”), a solid oxide electrolyzer cell (also referred to as“SOEC”), or a reversible SOFC-SOEC.
  • electrode can be an oxygen electrode.
  • the device can be a sensor device comprising the electrode described herein.
  • the sensor device is an amperometric sensor.
  • the sensor device is a potentiometric sensor.
  • Embodiment 1 An electrode comprising:
  • a functional layer comprising an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
  • the functional layer further comprising a ceria phase comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is greater than 0.2, y is in a range of 0 to 0.2, and x+y is greater than 0.4 and no greater than the solubility limit of ceria.
  • Embodiment 2 An electrode comprising: a functional layer comprising an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
  • the functional layer further comprising a ceria phase comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
  • At least one lanthanide of the Ln2MO4 phase is the same as at least one rare earth dopant of the ceria phase.
  • Embodiment 3 An electrode comprising:
  • a functional layer comprising an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
  • the functional layer further comprising a ceria phase comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
  • ceria phase is present in the functional layer in an amount of at least 40 vol% based on a total volume of the functional layer absent any porosity.
  • Embodiment 4 A method of forming an electrode, comprising:
  • Ln2MO4 material where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
  • a ceria material comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria;
  • Embodiment 5 The method of embodiment 4, wherein the sintering temperature is at least 1100°C, or at least 1200°C, or at least 1300°C.
  • Embodiment 6 The electrode or method of any one of the preceding embodiments, wherein the lanthanide of the Ln2MO4 phase includes at least one of La, Sm, Er, Pr, Nd, Gd, Dy or any combination thereof.
  • Embodiment 7 The electrode or method of any one of the preceding embodiments, wherein the lanthanide of the Ln2MO4 phase is doped with an alkaline earth metal.
  • Embodiment 8 The electrode or method of any one of the preceding embodiments, wherein the lanthanide of the Ln2MO4 phase is doped with an alkaline earth metal including at least one of Sr, Ca, Ba, or any combination thereof.
  • Embodiment 9 The electrode or method of any one of the preceding embodiments, wherein the 3d transition metal of the Ln2MO4 phase includes at least one of Ni, Cu, Co, Fe, Mn or any combination thereof.
  • Embodiment 10 The electrode or method of any one of the preceding embodiments, wherein A is La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, or any combination thereof.
  • Embodiment 11 The electrode or method of any one of the preceding embodiments, wherein x+y is at least 0.41, or at least 0.42, or at least 0.43, or at least 0.44, or at least 0.45, or at least 0.46, or at least 0.47.
  • Embodiment 12 The electrode or method of any one of the preceding embodiments, wherein x+y is at most 0.5.
  • Embodiment 13 The electrode or method of any one of the preceding embodiments, wherein less than 5 vol% free rare earth oxide is detectable in the functional layer.
  • Embodiment 14 The electrode or method of any one of the preceding embodiments, wherein less than 5 vol% of 3d transition metal oxide is detectable in the functional layer.
  • Embodiment 15 The electrode or method of any one of the preceding embodiments, wherein the ceria phase is present in the functional layer in an amount of at least 40 vol%, or at least 45 vol%, or at least 50 vol%, or at least 55 vol%, or at least 60 vol%, or at least 65 vol%, or at least 70 vol%, or at least 75 vol%, based on a total volume of the functional layer minus porosity.
  • Embodiment 16 The electrode or method of any one of the preceding embodiments, wherein the functional layer has a porosity of at least 10 vol%, or at least 15 vol%, or at least 18 vol%, based on a total volume of the functional layer.
  • Embodiment 17 The electrode or method of any one of the preceding embodiments, wherein the functional layer has an porosity of at most 60 vol%, or at most 50 vol%, or at most 40 vol%, or at most 35 vol%, based on a total volume of the functional layer.
  • Embodiment 18 The electrode or method of any one of the preceding embodiments, wherein the functional layer has a thickness of at least 5 micron, or at least 10 microns, or at least 12 microns, or at least 15 microns, or at least 20 microns.
  • Embodiment 19 The electrode or method of any one of the preceding embodiments, wherein the functional layer has a thickness of at most 100 microns, at most 90 microns, at most 80 microns, or at most 70 microns.
  • Embodiment 20 The electrode or method of any one of the preceding embodiments, wherein the functional layer includes the Ln 2 MO 4 phase in an initial composition.
  • Embodiment 21 An electrochemical device comprising the electrode of any one of the preceding embodiments.
  • Embodiment 22 The electrochemical device of embodiment 21, wherein the electrochemical device is an SOFC, an SOEC, or a reversible SOFC-SOEC.
  • Embodiment 23 The electrochemical device of any one of embodiments 21 and 22, further comprising an electrolyte layer.
  • Embodiment 24 The electrochemical device of embodiment 23, wherein the electrolyte layer has a thickness of at most 800 microns, or at most 600 microns, or at most 400 microns, or at most 200 microns, or at most 50 microns.
  • Embodiment 25 The electrochemical device of any one of embodiments 23 and 24, wherein the electrolyte layer has a porosity of at most 10 vol%, or at most 8 vol%, or at most 6 vol%, or at most 4 vol%, based on a total volume of the electrolyte layer.
  • Embodiment 26 The electrochemical device of any one of embodiments 23 to 25, wherein the electrolyte layer comprises at least one of ceria, zirconia, lanthanum gallate or a combination thereof.
  • Embodiment 27 The electrochemical device of embodiment 26, wherein the electrolyte layer includes a doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.05, y is in a range of 0 to 0.1, and x+y is greater than 0 and less than 0.25.
  • Embodiment 28 The electrochemical device of embodiment 26, wherein the electrolyte layer includes a stabilized zirconia.
  • Embodiment 29 The electrochemical device of embodiment 28, further comprising a barrier layer disposed between the functional layer and the electrolyte layer.
  • Embodiment 30 The electrochemical device of embodiment 29, wherein the barrier layer includes doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.05, y is in a range of 0 to 0.2, and x+y is greater than 0.05 and no greater than the solubility limit of ceria.
  • Embodiment 31 The electrochemical device of embodiment 30, wherein A is La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, Pr, or any combination thereof.
  • Embodiment 32 The electrochemical device of any one of embodiments 29 to 31, wherein the barrier layer has a porosity of at most 15 vol%, or at most 12 vol%, or at most 10 vol%.
  • Embodiment 33 The electrochemical device of any one of embodiments 29 to 32, wherein the barrier layer has a thickness less than the electrolyte layer and the functional layer.
  • Embodiment 34 The electrochemical device of any one of embodiments 22 to 33, wherein the electrochemical device is a solid oxide fuel cell and the electrode is an oxygen electrode.
  • Embodiment 35 The electrochemical device of embodiment 34, wherein the fuel electrode comprises a Ni-YSZ anode electrode.
  • Embodiment 36 The electrochemical device of any one of embodiments 22 to 33, wherein the electrochemical device is a solid oxide electrolyzer cell and the electrode is an anode electrode.
  • Embodiment 37 A sensor device comprising the electrode of any one of embodiments 1 to 20.
  • Embodiment 38 The sensor device of embodiment 37, wherein the sensor device is an amperometric sensor.
  • Embodiment 39 The sensor device of embodiment 37, wherein the sensor device is a potentiometric sensor.
  • SDC:LNO mixtures were mixed poly(ethylene glycol) 400 and poly(vinyl alcohol) 205 as a binder system to form a slurry. Each sample was prepared with 0.6 g of the slurry pressed at room temperature in a 6 mm diameter cylinder. After sintering, they were heated up to 1200°C and back down to room temperature at 2°C/min to measure the CTE.
  • the CTE reported in Table 1 is the value over the cooling down cycle in the range of 1200°C to 100°C.
  • the CTE of LNO-SDC mixtures described in Table 1 is low enough to be used for SOFC cathodes with YSZ as the electrolyte.
  • the initial composition included SDC as Sm 0.2 Ce 0.8 O 2 and LNO as La 2 NiO 4 . Table 1
  • Sample 2 was prepared identically to Sample 1 except SDC was replaced with LDC40, where the initial composition included LDC40 as La 0.40 Ce 0.60 O 2 and LNO as La 2 NiO 4 .
  • the results for Sample 2 are provided in Table 2.
  • Sample 3 included SDC-LNO compositions at 46:54 vol% SDC:LNO, 56:44 vol% SDC:LNO, and 66:34 vol% SDC:LNO, each after annealing at 1300°C for 5 hrs.
  • the initial composition for Sample 3 included a lightly-doped SDC phase (Sm 0.2 Ce 0.8 O 2 ), and an LNO phase (La 2 NiO 4 ).
  • the X-ray diffraction (XRD) patterns for Sample 3 are provided in the graph of FIG.1.
  • the amount of La incorporated in the ceria lattice could be estimated, by measuring lattice parameters from XRD patterns, as Because of the adsorption of La 2 O 3 in the ceria lattice, LNO is La 2 O 3 depleted, which leads to its decomposition and the formation of NiO.
  • Sample 4 included LDC30-LNO compositions at 77:23 vol% LDC30:LNO, 66:34 vol% LDC30:LNO, and 100:0 vol% LDC30:LNO, each after annealing at 1300°C for 5 hrs.
  • the initial composition for Sample 4 included LDC30 as La 0.30 Ce 0.70 O 2 and LNO as La 2 NiO 4 .
  • the XRD patterns for Sample 4 are provided in the graph of FIG.2, and shows that the peaks (more specifically (111) and (200)) of the lightly-doped ceria, which had been introduced as single-phase ceria, were split. This was not desirable as it indicated significant diffusion of La 2 O 3 from the LNO phase into the LDC lattice, meaning that the LNO phase is decomposed.
  • Sample 5 included LDC40-LNO compositions at 77:23 vol% LDC40:LNO, 66:34 vol% LDC40:LNO, and 100:0 vol% LDC40:LNO, each after annealing at 1300°C for 5 hrs.
  • the initial composition for Sample 5 included LDC40 as La 0.40 Ce 0.60 O 2 and LNO as La 2 NiO 4 .
  • the XRD patterns for Sample 5 are provided in the graph of FIG.3, showing there is no split peak.
  • Sample 6 is similar to Sample 5 except that it included LDC40-LNO compositions at 77:23 vol% LDC40:LNO, 66:34 vol% LDC40:LNO, 56:44 vol% LDC40:LNO, and 46:54 vol% LDC40:LNO.
  • the initial composition for Sample 6 included LDC40 as La 0.40 Ce 0.60 O 2 and LNO as La 2 NiO 4 .
  • the XRD patterns for Sample 6 are provided in the graph of FIG.4, and are measured at a scale sufficient to show there was no extra peak indicating any decomposition of LNO or formation of NiO.
  • Sample 7 included LDC48-LNO compositions at 77:23 vol% LDC48:LNO, 66:34 vol% LDC48:LNO, and 100:0 vol% LDC48:LNO, each after annealing at 1300°C for 5 hrs.
  • the initial composition of Sample 7 includes LDC48 as La 0.48 Ce 0.52 O 2 and LNO as La 2 NiO 4 .
  • the XRD patterns are provided in the graph of FIG.5.
  • Samples 8, 9 and 10 below showed the stability of NNO and LSNO phases in the presence of a heavily-doped ceria phase.
  • Sample 8 included NDC43-NNO compositions at 60:40 vol% NDC43:NNO and 80:20 vol% NDC43:NNO, each after annealing at 1300°C for 5 hrs.
  • the initial composition of Sample 8 included NDC43 as Nd 0.43 Ce 0.57 O 2 and NNO as Nd 2 NiO 4 .
  • the X-ray diffraction results are provided in the graph of FIG.6, and show the stability of NNO even in low NNO volume fractions, using a composite having a heavily-doped ceria phase.
  • Sample 9 included LDC40-LSNO compositions at 50:50 vol% LDC40:LSNO, 60:40 vol% LDC40:LSNO, 70:30 vol% LDC40:LSNO, and 80:20 vol% LDC40:LSNO, each after annealing at 1300°C for 5 hrs.
  • the initial composition of Sample 9 included LDC40 as La 0.40 Ce 0.60 O 2 and LSNO as La 1.8 Sr 0.2 NiO 4 .
  • the X-ray diffraction patterns are provided in the graph of FIG.7, and show the stability of LSNO, even in low LSNO volume fractions, using a composite having a heavily-doped ceria phase.
  • Sample 10 included LDC48-NNO compositions at 50:50 vol% LDC48:NNO, 60:40 vol% LDC48:NNO, and 80:20 vol% LDC48:NNO, each after annealing at 1300°C for 5 hrs.
  • the initial composition for Sample 10 included LDC48 as La 0.48 Ce 0.52 O 2 and NNO as Nd 2 NiO 4 .
  • the X-ray diffraction patterns are provided in the graph of FIG.8, and show the stability of NNO, even in low NNO volume fractions, using a composite having a heavily- doped ceria phase with a different rare earth dopant.
  • a solid oxide fuel cell was prepared using a Ni-YSZ anode, YSZ electrolyte, SDC barrier layer, and LNO-LDC40 cathode functional layer.
  • the thickness of the LNO-LDC40 cathode functional layer was about 20 to 30 ⁇ m.
  • the porosity of the cathode functional layer was about 15%.
  • a substantially dense SDC barrier layer was placed between the YSZ electrolyte and the functional layer to avoid the formation of any insulating phase between the electrolyte and the cathode functional layer.
  • the thickness of the SDC barrier layer was about 3 ⁇ m and its porosity was about 3%.
  • FIG.8 An SEM image of the multilayer fuel cell is provided in FIG.8 and the performance characteristics of the SOFC button cell demonstrating high performance are provided in the graph of FIG.9. Note that not all of the activities described above in the general description or the examples are required, that a portion of a specific activity may not be required, and that one or more further activities may be performed in addition to those described. Still further, the order in which activities are listed is not necessarily the order in which they are performed.

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Abstract

An electrode can include a functional layer having an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal, and a heavily-doped ceria phase. An electrochemical device or a sensor device can include the electrode.

Description

ELECTRODE COMPRISING HEAVILY-DOPED CERIA
TECHNICAL FIELD
The present disclosure relates to electrodes and devices comprising the electrodes. BACKGROUND ART
In the context of solid oxide fuel and electrolyzer cells, operating temperatures greater than 700°C are desirable for the more facile kinetics of the gas reactants and lower resistance of the ionic membrane. High operating temperatures also allow internal reformation of hydrocarbon fuels, which can reduce the system size significantly compared to systems with external reforming. However, the high operating temperatures can reduce electrode performance. A need exists for an improved electrode material.
BRIEF DESCRIPTION OF THE DRAWINGS
Embodiments are illustrated by way of example and are not limited in the
accompanying figures.
FIGs.1 to 8 include graphs of XRD patterns for various Samples described in the Examples.
FIG.9 includes a photograph of an SOFC button cell described in the Examples. FIG.10 includes a graph of performance characteristics of the SOFC button cell of FIG.9.
Skilled artisans appreciate that elements in the figures are illustrated for simplicity and clarity and have not necessarily been drawn to scale. For example, the dimensions of some of the elements in the figures may be exaggerated relative to other elements to help to improve understanding of embodiments of the invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT(S)
The following description in combination with the figures is provided to assist in understanding the teachings disclosed herein. The following discussion will focus on specific implementations and embodiments of the teachings. This focus is provided to assist in describing the teachings and should not be interpreted as a limitation on the scope or applicability of the teachings. However, other embodiments can be used based on the teachings as disclosed in this application.
The terms“comprises,”“comprising,”“includes,”“including,”“has,”“having” or any other variation thereof, are intended to cover a non-exclusive inclusion. For example, a method, article, or apparatus that comprises a list of features is not necessarily limited only to those features but may include other features not expressly listed or inherent to such method, article, or apparatus. Further, unless expressly stated to the contrary,“or” refers to an inclusive-or and not to an exclusive-or. For example, a condition A or B is satisfied by any one of the following: A is true (or present) and B is false (or not present), A is false (or not present) and B is true (or present), and both A and B are true (or present).
Also, the use of“a” or“an” is employed to describe elements and components described herein. This is done merely for convenience and to give a general sense of the scope of the invention. This description should be read to include one, at least one, or the singular as also including the plural, or vice versa, unless it is clear that it is meant otherwise. For example, when a single item is described herein, more than one item may be used in place of a single item. Similarly, where more than one item is described herein, a single item may be substituted for that more than one item.
Unless otherwise stated, the term“vol%,” when used herein to describe the composition of a layer, refers to a percentage of the total volume of the solids, e.g., excluding porosity, of the layer. Further, unless otherwise stated, the term“mol%,” when used herein to describe a dopant concentration, refers to a percentage of the total amount, in moles, of cations in a given compound. Furthermore, the oxygen stoichiometry in any of the formulas provided below may vary slightly and, thus, is considered to include a delta (excess or deficiency), referred to as“d”, of +/- 0.5. In particular, a doped ceria (CeABO(2-d)) can have oxygen understoichiometry (oxygen deficiency) where d is a deficiency of at most 0.29, at most 0.27, or at most 0.25; and an Ln2MO4+d can have oxygen overstoichiometry (oxygen excess) where d is an excess of at most 0.34, at most 0.32, or at most 0.3. For example, La0.40Ce0.60O2 would include, e.g., La0.40Ce0.60O2-d, where d is at at most 0.25, and La2NiO4+d would include, e.g., La2NiO4+d, where d is at most 0.3.
Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The materials, methods, and examples are illustrative only and not intended to be limiting. To the extent not described herein, many details regarding specific materials and processing acts are conventional and may be found in textbooks and other sources within the electrochemical arts.
An electrode can include a composite functional layer including a heavily-doped ceria that is suitable for operating temperatures of greater than 700°C. As used herein, the term “heavily-doped” refers to a dopant concentration of at least 40 mol%. In an embodiment, the electrode can include a first phase comprising the heavily-doped ceria and a second phase including an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal, without the reactivity problems encountered with existing composite electrode materials. The concepts are better understood in view of the embodiments described below that illustrate and do not limit the scope of the present invention
High temperature electrochemical cells can include a number of requirements for high performance. Ideally, the materials should withstand processing temperatures of at least 1000°C without decomposing or forming resistive phases and maintain a stable composition and crystal structure at operating conditions. In addition, the functional layers should retain porosity and facile electron transfer reaction kinetics.
Ln2MO4 materials can generally provide high electrode performance, where Ln is any of the lanthanide elements and M is a 3d transition metal. In particular, the Ln2MO4 family of materials can offer a wider operating temperature range (e.g., 700°C to 900°C) as compared to other materials only suitable for either higher or lower temperatures. The Ln2MO4 family of materials provides the additional advantage of mixed ionic electronic conductivity.
However, the Ln2MO4 family of materials can be reactive with common high temperature electrolytes. Moreover, Ln2MO4 materials have a high coefficient of thermal expansion (referred to herein as“CTE”), reducing mechanical stability in a multilayer architecture.
A rare earth-doped ceria can form a composite with the Ln2MO4 materials to form a composite electrode with a reduced CTE. However, a lightly-doped ceria can react with Ln2MO4 when in intimate contact at elevated temperatures. As used herein, the term“lightly- doped” refers to a dopant concentration of less than 40 mol%.
Applicants have discovered that an Ln2MO4:ceria composite including a heavily- doped ceria, especially near the solubility limit of ceria, surprisingly does not exhibit the same reactivity as the lightly-doped ceria. The solubility limit is the amount of rare earth oxide that can be incorporated into the ceria lattice while maintaining its fluorite structure. Further, diffusional transport of the lanthanide element from the Ln2MO4 into the ceria is suppressed since the dopant concentration is close to the solubility limit of Ln in ceria.
As discussed above, the Ln of the Ln2MO4 phase includes at least one lanthanide. In an embodiment, the Ln of the Ln2MO4 phase includes at least one lanthanide selected from the group consisting of La, Sm, Er, Pr, Nd, Gd, Dy, or any combination thereof. Further, the at least one lanthanide or combination thereof can be doped with a metal. The metal dopant can include an alkaline earth metal. In a particular embodiment, the alkaline earth metal can include at least one alkaline earth selected from the group consisting of Sr, Ca, Ba, or any combination thereof to increase hole conductivity.
Further, as discussed above, the M of the Ln2MO4 phase includes a 3d transition metal. In an embodiment, the M of the Ln2MO4 phase includes at least one 3d transition metal selected from the group consisting of Ni, Cu, Co, Fe, Mn or any combination thereof.
The heavily-doped ceria phase can include a ceria and at least one dopant such that the total dopant concentration is at least 40 mol% and no greater than the solubility limit of ceria. In an embodiment, the heavily-doped ceria can have the general formula:
Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
In an embodiment, the rare earth dopant A includes at least one dopant selected from the group consisting of La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, or any combination thereof. In a more particular embodiment, the rare earth dopant A includes at least one of La, Gd, Nd, or Sm. In a further embodiment, x+y is at least 0.4, or greater than 0.4, or at least 0.41, or at least 0.42, or at least 0.43, or at least 0.44, or at least 0.45, or at least 0.46, or at least 0.47. It would be expected that the use of heavily-doped ceria for cathode functional layers would lead to lower ionic conductivity. In addition, current literature indicates that electrode performance decreases as x+y increases up to 0.4. See, for example, Figure 11 of Perez-Coll, et al.,“Optimization of the interface polarization of the La2NiO4-based cathode working with the
Figure imgf000006_0001
electrolyte system.” However, Applicant has discovered that, contrary to Perez-Coll et al., as x+y increases to 40 mol% or greater, even up to the solubility limit of ceria, the more thermodynamically stable the phase is and the diffusion of the lanthanide element from Ln2MO4 is reduced. That being said, the benefits of increasing the dopant concentration begin to deteriorate beyond the solubility limit of ceria. In further
embodiments, x+y is no greater than the solubility limit. In a particular embodiment, x+y is no greater than 0.5.
In an embodiment, the alkaline earth dopant B includes at least one dopant selected from the group consisting of Sr, Ca, Ba, or any combination thereof. In a further
embodiment, y can be 0, meaning that the heavily-doped ceria phase does not include an alkaline earth dopant B. In other embodiments, y is at least 0.01, or at least 0.05, or at least 0.1. In other embodiments, y is at most 0.24, or at most 0.22, or at most 0.2.
As mentioned previously, a lightly-doped ceria phase can be reactive with an Ln2MO4 phase. Such a reaction can cause diffusion of the Ln into the lightly-doped ceria, leading to a reduction or even a complete removal of the Ln from the Ln2MO4 phase. In addition, such a reaction can lead to the presence of a metal oxide (MO) and/or a free rare earth oxide (RE2O3), which were not initially present in the electrode, particularly when M is Ni.
However, in the composite electrode described herein, the reactivity is reduced or avoided such that, in an embodiment, less than 5 vol% of free RE2O3 rare earth oxide is detectable in the functional layer of the electrode. In an embodiment, less than 5 vol% of MO metal oxide is detectable in the functional layer of the electrode. The detection method is x-ray diffraction having a detection limit of 5 vol%.
In an embodiment, the ceria phase can be present in the functional layer of the electrode in an amount of at least 40 vol%, or at least 45 vol%, or at least 50 vol%, or at least 55 vol%, or at least 60 vol%, or at least 65 vol%, or at least 70 vol%, or at least 75 vol%, based on a total volume of the functional layer minus the volume occupied by porosity. For a lightly-doped ceria phase, increasing the volume percent of the ceria phase would increase the likelihood of rare earth diffusion. Thus, higher performance for composite electrodes including a lightly-doped ceria phase would be exhibited at lower concentrations of the ceria phase. On the other hand, as the heavily-doped ceria is near the solubility limit of ceria, the thermodynamic stability is increased and, thus, the volume percent of the ceria phase can be increased without increasing the likelihood of rare earth diffusion.
In an embodiment, the functional layer of the electrode has a porosity of at least 10 vol%, or at least 15 vol%, or at least 18 vol%, based on a total volume of the functional layer. Further, in an embodiment, the functional layer of the electrode has a porosity of at most 60 vol%, or at most 50 vol%, or at most 40 vol%, or at most 35 vol%, based on a total volume of the functional layer. The porosity is determined by image analysis of the cross section of the layer using an image analysis tool such as ImageJ to view and measure the porosity by contrast.
In an embodiment, the functional layer of the electrode has the functional layer has a thickness of at least 5 micron, or at least 10 microns, or at least 12 microns, or at least 15 microns, or at least 20 microns. Further, in an embodiment, the functional layer of the electrode has a thickness of at most 100 microns, at most 90 microns, at most 80 microns, or at most 70 microns.
The electrode described herein can be made by providing starter materials, mixing the starter materials, and sintering the mixture. In an embodiment, the starter materials include an Ln2MO4 material, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal, and a ceria material comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
In an embodiment, a binder system can be added to the
Figure imgf000008_0001
material and the ceria material to form a slurry. In an embodiment, the binder system can include at least one polymer. The slurry can be deposited by a ceramic forming technique such as spraying, tape casting or screen printing and then sintered to form an electrode having an Ln2MO4 phase and a ceria phase. The sintering temperature can be greater than the operating temperature. For example, the sintering temperature can be at least 1000°C, or at least 1100°C, or at least 1200°C, or at least 1300°C. In an embodiment, the sintering temperature can be no greater than 1800°C, or no greater than 1700°C, or no greater than 1600°C.
The electrode described herein can be utilized as a component in a variety of devices including electrochemical devices, sensor devices, and the like.
In an embodiment, the electrochemical device including the electrode described herein comprises an electrolyte layer, an optional barrier layer, and an anode layer. The electrolyte layer can comprise at least one electrolyte material selected from the group consisting of ceria, zirconia, lanthanum gallate, or a combination thereof.
In a particular embodiment, the electrolyte material includes a stabilized zirconia. In a particular embodiment, the electrolyte layer includes a doped ceria having the general formula:
Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.05, y is in a range of 0 to 0.1, and x+y is greater than 0.05 and less than 0.25. In a particular embodiment, A is La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, or any combination thereof. In a particular embodiment, B is Sr, Ca, Ba, or any combination thereof.
The electrolyte layer can have a thickness of at most 800 microns, or at most 600 microns, or at most 400 microns, or at most 200 microns, or at most 50 microns. Further, the electrolyte layer can have a thickness of at least 1 micron, at least 3 microns, or at least 5 microns.
The electrolyte layer can have a porosity of at most 10 vol%, or at most 8 vol%, or at most 6 vol%, or at most 4 vol%, based on a total volume of the electrolyte layer. Further, while the electrolyte may be completely dense, it is possible that some porosity can exist, such as at least 0.01 vol%, or at least 0.05 vol%, or at least 0.1 vol%. In an embodiment, the electrochemical device includes a barrier layer disposed between the electrode and the electrolyte layer. In a particular embodiment, the barrier layer includes doped ceria having the general formula:
Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.05, y is in a range of 0 to 0.2, and x+y is greater than 0.05 and no greater than the solubility limit of ceria. In a particular embodiment, A is La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, Pr, or any combination thereof. In a particular embodiment, B is Sr, Ca, Ba, or any combination thereof.
In an embodiment, the barrier layer has a porosity of at most 15 vol%, or at most 12 vol%, or at most 10 vol%, based on a total volume of the barrier layer. In an embodiment, the barrier layer has a porosity of at least 0.5 vol%, or at least 1 vol%, or at least 2 vol%, or at least 3 vol%, based on a total volume of the barrier layer.
In an embodiment, the barrier layer has a thickness less than the electrolyte layer and the functional layer.
In a particular embodiment, the electrochemical device includes a solid oxide fuel cell (also referred to as“SOFC”), a solid oxide electrolyzer cell (also referred to as“SOEC”), or a reversible SOFC-SOEC. In a particular embodiment, electrode can be an oxygen electrode.
Moreover, the device can be a sensor device comprising the electrode described herein. In a particular embodiment, the sensor device is an amperometric sensor. In another embodiment, the sensor device is a potentiometric sensor.
Many different aspects and embodiments are possible. Some of those aspects and embodiments are described below. After reading this specification, skilled artisans will appreciate that those aspects and embodiments are only illustrative and do not limit the scope of the present invention. Embodiments may be in accordance with any one or more of the items as embodiments below.
Embodiment 1. An electrode comprising:
a functional layer comprising an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
the functional layer further comprising a ceria phase comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is greater than 0.2, y is in a range of 0 to 0.2, and x+y is greater than 0.4 and no greater than the solubility limit of ceria.
Embodiment 2. An electrode comprising: a functional layer comprising an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
the functional layer further comprising a ceria phase comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
wherein at least one lanthanide of the Ln2MO4 phase is the same as at least one rare earth dopant of the ceria phase.
Embodiment 3. An electrode comprising:
a functional layer comprising an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
the functional layer further comprising a ceria phase comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
wherein the ceria phase is present in the functional layer in an amount of at least 40 vol% based on a total volume of the functional layer absent any porosity.
Embodiment 4. A method of forming an electrode, comprising:
providing an Ln2MO4 material, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
providing a ceria material comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria;
mixing the Ln2MO4 material and the ceria material to form a mixture; and sintering the mixture at a temperature that is at least 1000 °C and greater than the operating temperature to form a functional layer of the oxygen electrode having an Ln2MO4 phase and a ceria phase.
Embodiment 5. The method of embodiment 4, wherein the sintering temperature is at least 1100°C, or at least 1200°C, or at least 1300°C.
Embodiment 6. The electrode or method of any one of the preceding embodiments, wherein the lanthanide of the Ln2MO4 phase includes at least one of La, Sm, Er, Pr, Nd, Gd, Dy or any combination thereof. Embodiment 7. The electrode or method of any one of the preceding embodiments, wherein the lanthanide of the Ln2MO4 phase is doped with an alkaline earth metal.
Embodiment 8. The electrode or method of any one of the preceding embodiments, wherein the lanthanide of the Ln2MO4 phase is doped with an alkaline earth metal including at least one of Sr, Ca, Ba, or any combination thereof.
Embodiment 9. The electrode or method of any one of the preceding embodiments, wherein the 3d transition metal of the Ln2MO4 phase includes at least one of Ni, Cu, Co, Fe, Mn or any combination thereof.
Embodiment 10. The electrode or method of any one of the preceding embodiments, wherein A is La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, or any combination thereof.
Embodiment 11. The electrode or method of any one of the preceding embodiments, wherein x+y is at least 0.41, or at least 0.42, or at least 0.43, or at least 0.44, or at least 0.45, or at least 0.46, or at least 0.47.
Embodiment 12. The electrode or method of any one of the preceding embodiments, wherein x+y is at most 0.5.
Embodiment 13. The electrode or method of any one of the preceding embodiments, wherein less than 5 vol% free rare earth oxide is detectable in the functional layer.
Embodiment 14. The electrode or method of any one of the preceding embodiments, wherein less than 5 vol% of 3d transition metal oxide is detectable in the functional layer.
Embodiment 15. The electrode or method of any one of the preceding embodiments, wherein the ceria phase is present in the functional layer in an amount of at least 40 vol%, or at least 45 vol%, or at least 50 vol%, or at least 55 vol%, or at least 60 vol%, or at least 65 vol%, or at least 70 vol%, or at least 75 vol%, based on a total volume of the functional layer minus porosity.
Embodiment 16. The electrode or method of any one of the preceding embodiments, wherein the functional layer has a porosity of at least 10 vol%, or at least 15 vol%, or at least 18 vol%, based on a total volume of the functional layer.
Embodiment 17. The electrode or method of any one of the preceding embodiments, wherein the functional layer has an porosity of at most 60 vol%, or at most 50 vol%, or at most 40 vol%, or at most 35 vol%, based on a total volume of the functional layer.
Embodiment 18. The electrode or method of any one of the preceding embodiments, wherein the functional layer has a thickness of at least 5 micron, or at least 10 microns, or at least 12 microns, or at least 15 microns, or at least 20 microns. Embodiment 19. The electrode or method of any one of the preceding embodiments, wherein the functional layer has a thickness of at most 100 microns, at most 90 microns, at most 80 microns, or at most 70 microns.
Embodiment 20. The electrode or method of any one of the preceding embodiments, wherein the functional layer includes the Ln2MO4 phase in an initial composition.
Embodiment 21. An electrochemical device comprising the electrode of any one of the preceding embodiments.
Embodiment 22. The electrochemical device of embodiment 21, wherein the electrochemical device is an SOFC, an SOEC, or a reversible SOFC-SOEC.
Embodiment 23. The electrochemical device of any one of embodiments 21 and 22, further comprising an electrolyte layer.
Embodiment 24. The electrochemical device of embodiment 23, wherein the electrolyte layer has a thickness of at most 800 microns, or at most 600 microns, or at most 400 microns, or at most 200 microns, or at most 50 microns.
Embodiment 25. The electrochemical device of any one of embodiments 23 and 24, wherein the electrolyte layer has a porosity of at most 10 vol%, or at most 8 vol%, or at most 6 vol%, or at most 4 vol%, based on a total volume of the electrolyte layer.
Embodiment 26. The electrochemical device of any one of embodiments 23 to 25, wherein the electrolyte layer comprises at least one of ceria, zirconia, lanthanum gallate or a combination thereof.
Embodiment 27. The electrochemical device of embodiment 26, wherein the electrolyte layer includes a doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.05, y is in a range of 0 to 0.1, and x+y is greater than 0 and less than 0.25.
Embodiment 28. The electrochemical device of embodiment 26, wherein the electrolyte layer includes a stabilized zirconia.
Embodiment 29. The electrochemical device of embodiment 28, further comprising a barrier layer disposed between the functional layer and the electrolyte layer.
Embodiment 30. The electrochemical device of embodiment 29, wherein the barrier layer includes doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.05, y is in a range of 0 to 0.2, and x+y is greater than 0.05 and no greater than the solubility limit of ceria.
Embodiment 31. The electrochemical device of embodiment 30, wherein A is La, Gd, Nd, Sm, Dy, Er, Y, Yb, Ho, Pr, or any combination thereof. Embodiment 32. The electrochemical device of any one of embodiments 29 to 31, wherein the barrier layer has a porosity of at most 15 vol%, or at most 12 vol%, or at most 10 vol%.
Embodiment 33. The electrochemical device of any one of embodiments 29 to 32, wherein the barrier layer has a thickness less than the electrolyte layer and the functional layer.
Embodiment 34. The electrochemical device of any one of embodiments 22 to 33, wherein the electrochemical device is a solid oxide fuel cell and the electrode is an oxygen electrode.
Embodiment 35. The electrochemical device of embodiment 34, wherein the fuel electrode comprises a Ni-YSZ anode electrode.
Embodiment 36. The electrochemical device of any one of embodiments 22 to 33, wherein the electrochemical device is a solid oxide electrolyzer cell and the electrode is an anode electrode.
Embodiment 37. A sensor device comprising the electrode of any one of embodiments 1 to 20.
Embodiment 38. The sensor device of embodiment 37, wherein the sensor device is an amperometric sensor.
Embodiment 39. The sensor device of embodiment 37, wherein the sensor device is a potentiometric sensor.
Examples
Example 1: Coefficient of Thermal Expansion
The CTE of various samples were measured.
For Sample 1, SDC:LNO mixtures were mixed poly(ethylene glycol) 400 and poly(vinyl alcohol) 205 as a binder system to form a slurry. Each sample was prepared with 0.6 g of the slurry pressed at room temperature in a 6 mm diameter cylinder. After sintering, they were heated up to 1200°C and back down to room temperature at 2°C/min to measure the CTE. The CTE reported in Table 1 is the value over the cooling down cycle in the range of 1200°C to 100°C. The CTE of LNO-SDC mixtures described in Table 1 is low enough to be used for SOFC cathodes with YSZ as the electrolyte. For Sample 1, the initial composition included SDC as Sm0.2Ce0.8O2 and LNO as La2NiO4. Table 1
Figure imgf000014_0002
Sample 2 was prepared identically to Sample 1 except SDC was replaced with LDC40, where the initial composition included LDC40 as La0.40Ce0.60O2 and LNO as La2NiO4. The results for Sample 2 are provided in Table 2.
Table 2
Figure imgf000014_0003
similar to Sample 1. However, unlike Sample 1, the CTE values for heavily-doped ceria in Sample 2 follow here the rule of mixture, which further indicates that the phases for Sample 2 are thermodynamically stable.
Example 2: X-ray Diffraction
Sample 3 included SDC-LNO compositions at 46:54 vol% SDC:LNO, 56:44 vol% SDC:LNO, and 66:34 vol% SDC:LNO, each after annealing at 1300°C for 5 hrs. The initial composition for Sample 3 included a lightly-doped SDC phase (Sm0.2Ce0.8O2), and an LNO phase (La2NiO4). The X-ray diffraction (XRD) patterns for Sample 3 are provided in the graph of FIG.1. In the case of the 66:34 vol% SDC:LNO mixture, the amount of La incorporated in the ceria lattice could be estimated, by measuring lattice parameters from XRD patterns, as
Figure imgf000014_0001
Because of the adsorption of La2O3 in the ceria lattice, LNO is La2O3 depleted, which leads to its decomposition and the formation of NiO.
Sample 4 included LDC30-LNO compositions at 77:23 vol% LDC30:LNO, 66:34 vol% LDC30:LNO, and 100:0 vol% LDC30:LNO, each after annealing at 1300°C for 5 hrs. The initial composition for Sample 4 included LDC30 as La0.30Ce0.70O2 and LNO as La2NiO4. The XRD patterns for Sample 4 are provided in the graph of FIG.2, and shows that the peaks (more specifically (111) and (200)) of the lightly-doped ceria, which had been introduced as single-phase ceria, were split. This was not desirable as it indicated significant diffusion of La2O3 from the LNO phase into the LDC lattice, meaning that the LNO phase is decomposed.
However, when LDC (lanthanum-doped ceria) was introduced with a concentration of dopant at or above 40 vol%, and below the solubility limit of ceria, around 50 mol%, the peaks of doped ceria are not split, as it can be seen below in the case of 40 mol% (Sample 5 and 6 below), and 48 mol% (Sample 7 below). The closer the dopant concentration was to the solubility limit, the results were more desirable, as the XRD patterns indicated the composite was more thermodynamically stable.
Sample 5 included LDC40-LNO compositions at 77:23 vol% LDC40:LNO, 66:34 vol% LDC40:LNO, and 100:0 vol% LDC40:LNO, each after annealing at 1300°C for 5 hrs. The initial composition for Sample 5 included LDC40 as La0.40Ce0.60O2 and LNO as La2NiO4. The XRD patterns for Sample 5 are provided in the graph of FIG.3, showing there is no split peak.
Sample 6 is similar to Sample 5 except that it included LDC40-LNO compositions at 77:23 vol% LDC40:LNO, 66:34 vol% LDC40:LNO, 56:44 vol% LDC40:LNO, and 46:54 vol% LDC40:LNO. Like Sample 5, the initial composition for Sample 6 included LDC40 as La0.40Ce0.60O2 and LNO as La2NiO4. The XRD patterns for Sample 6 are provided in the graph of FIG.4, and are measured at a scale sufficient to show there was no extra peak indicating any decomposition of LNO or formation of NiO.
Sample 7 included LDC48-LNO compositions at 77:23 vol% LDC48:LNO, 66:34 vol% LDC48:LNO, and 100:0 vol% LDC48:LNO, each after annealing at 1300°C for 5 hrs. The initial composition of Sample 7 includes LDC48 as La0.48Ce0.52O2 and LNO as La2NiO4. The XRD patterns are provided in the graph of FIG.5.
Samples 8, 9 and 10 below showed the stability of NNO and LSNO phases in the presence of a heavily-doped ceria phase.
Sample 8 included NDC43-NNO compositions at 60:40 vol% NDC43:NNO and 80:20 vol% NDC43:NNO, each after annealing at 1300°C for 5 hrs. The initial composition of Sample 8 included NDC43 as Nd0.43Ce0.57O2 and NNO as Nd2NiO4. The X-ray diffraction results are provided in the graph of FIG.6, and show the stability of NNO even in low NNO volume fractions, using a composite having a heavily-doped ceria phase.
Sample 9 included LDC40-LSNO compositions at 50:50 vol% LDC40:LSNO, 60:40 vol% LDC40:LSNO, 70:30 vol% LDC40:LSNO, and 80:20 vol% LDC40:LSNO, each after annealing at 1300°C for 5 hrs. The initial composition of Sample 9 included LDC40 as La0.40Ce0.60O2 and LSNO as La1.8Sr0.2NiO4. The X-ray diffraction patterns are provided in the graph of FIG.7, and show the stability of LSNO, even in low LSNO volume fractions, using a composite having a heavily-doped ceria phase.
Sample 10 included LDC48-NNO compositions at 50:50 vol% LDC48:NNO, 60:40 vol% LDC48:NNO, and 80:20 vol% LDC48:NNO, each after annealing at 1300°C for 5 hrs. The initial composition for Sample 10 included LDC48 as La0.48Ce0.52O2 and NNO as Nd2NiO4. The X-ray diffraction patterns are provided in the graph of FIG.8, and show the stability of NNO, even in low NNO volume fractions, using a composite having a heavily- doped ceria phase with a different rare earth dopant.
For each of Samples 3 to 10, the densities listed in Table 3 were calculated based on XRD patterns of the single phase materials, and used in the calculations for the vol% of the different mixtures.
Table 3
Figure imgf000016_0001
Example 3: SOFC Button Cell
A solid oxide fuel cell was prepared using a Ni-YSZ anode, YSZ electrolyte, SDC barrier layer, and LNO-LDC40 cathode functional layer. The thickness of the LNO-LDC40 cathode functional layer was about 20 to 30µm. The porosity of the cathode functional layer was about 15%. In addition, a substantially dense SDC barrier layer was placed between the YSZ electrolyte and the functional layer to avoid the formation of any insulating phase between the electrolyte and the cathode functional layer. The thickness of the SDC barrier layer was about 3µm and its porosity was about 3%. An SEM image of the multilayer fuel cell is provided in FIG.8 and the performance characteristics of the SOFC button cell demonstrating high performance are provided in the graph of FIG.9. Note that not all of the activities described above in the general description or the examples are required, that a portion of a specific activity may not be required, and that one or more further activities may be performed in addition to those described. Still further, the order in which activities are listed is not necessarily the order in which they are performed.
Benefits, other advantages, and solutions to problems have been described above with regard to specific embodiments. However, the benefits, advantages, solutions to problems, and any feature(s) that may cause any benefit, advantage, or solution to occur or become more pronounced are not to be construed as a critical, required, or essential feature of any or all the claims.
The specification and illustrations of the embodiments described herein are intended to provide a general understanding of the structure of the various embodiments. The specification and illustrations are not intended to serve as an exhaustive and comprehensive description of all of the elements and features of apparatus and systems that use the structures or methods described herein. Separate embodiments may also be provided in combination in a single embodiment, and conversely, various features that are, for brevity, described in the context of a single embodiment, may also be provided separately or in any subcombination. Further, reference to values stated in ranges includes each and every value within that range. Many other embodiments may be apparent to skilled artisans only after reading this specification. Other embodiments may be used and derived from the disclosure, such that a structural substitution, logical substitution, or another change may be made without departing from the scope of the disclosure. Accordingly, the disclosure is to be regarded as illustrative rather than restrictive.

Claims

WHAT IS CLAIMED IS:
1. An electrode comprising:
a functional layer comprising an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
the functional layer further comprising a ceria phase comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is greater than 0.2, y is in a range of 0 to 0.2, and x+y is greater than 0.4 and no greater than the solubility limit of ceria.
2. An electrode comprising:
a functional layer comprising an Ln2MO4 phase, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
the functional layer further comprising a ceria phase comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria.
wherein the ceria phase is present in the functional layer in an amount of at least 40 vol% based on a total volume of the functional layer absent any porosity.
3. A method of forming an electrode, comprising:
providing an Ln2MO4 material, where Ln is at least one lanthanide optionally doped with a metal and M is at least one 3d transition metal;
providing a ceria material comprising doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.2, y is in a range of 0 to 0.2, and x+y is at least 0.4 and no greater than the solubility limit of ceria;
mixing the Ln2MO4 material and the ceria material to form a mixture; and sintering the mixture at a temperature that is at least 1000 °C and greater than the operating temperature to form a functional layer of the oxygen electrode having an Ln2MO4 phase and a ceria phase.
4. The electrode or method of any one of the preceding claims, wherein the lanthanide of the Ln2MO4 phase is doped with an alkaline earth metal.
5. The electrode or method of any one of the preceding claims, wherein the 3d transition metal of the Ln2MO4 phase includes at least one of Ni, Cu, Co, Fe, Mn or any combination thereof.
6. The electrode or method of any one of the preceding claims, wherein x+y is at least 0.41, or at least 0.42, or at least 0.43, or at least 0.44, or at least 0.45, or at least 0.46, or at least 0.47.
7. The electrode or method of any one of the preceding claims, wherein x+y is at most 0.5.
8. The electrode or method of any one of the preceding claims, wherein less than 5 vol% of 3d transition metal oxide is detectable in the functional layer.
9. The electrode or method of any one of the preceding claims, wherein the ceria phase is present in the functional layer in an amount of at least 40 vol%, or at least 45 vol%, or at least 50 vol%, or at least 55 vol%, or at least 60 vol%, or at least 65 vol%, or at least 70 vol%, or at least 75 vol%, based on a total volume of the functional layer minus porosity.
10. An electrochemical device comprising the electrode of any one of the preceding claims.
11. The electrochemical device of claim 10, wherein the device comprises an electrolyte layer and the electrolyte layer comprises at least one of ceria, zirconia, lanthanum gallate or a combination thereof.
12. The electrochemical device of claim 11, wherein the electrolyte layer includes a doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.05, y is in a range of 0 to 0.1, and x+y is greater than 0 and less than 0.25.
13. The electrochemical device of claim 11, wherein the electrolyte layer comprises a stabilized zirconia and the device further comprises a barrier layer disposed between the functional layer and the electrolyte layer.
14. The electrochemical device of claim 13, wherein the barrier layer includes doped ceria having the general formula Ce(1-x-y)AxByO2, where A is at least one rare earth dopant, B is at least one alkaline earth dopant, x is at least 0.05, y is in a range of 0 to 0.2, and x+y is greater than 0.05 and no greater than the solubility limit of ceria.
15. A sensor device comprising the electrode of any one of claims 1 to 9.
PCT/US2017/034534 2016-05-25 2017-05-25 Electrode comprising heavily-doped ceria Ceased WO2017205660A1 (en)

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Families Citing this family (5)

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EP3686966A1 (en) 2019-01-23 2020-07-29 Karlsruher Institut für Technologie An electrochemical energy storage device and a method for producing an anode active material for the electrochemical energy storage device
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CN114045520B (en) * 2021-12-15 2023-05-26 中国科学院大连化学物理研究所 Oxygen electrode for solid oxide electrolysis hydrogen production and preparation method thereof
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010232135A (en) * 2009-03-30 2010-10-14 Mitsubishi Materials Corp Durable fuel electrode and solid oxide fuel cell incorporating this fuel electrode
US20120064433A1 (en) * 2010-09-14 2012-03-15 Samsung Electro-Mechanics Co., Ltd. Material for solid oxide fuel cell, cathode including the material, and solid oxide fuel cell including the material
KR20120123639A (en) * 2011-04-19 2012-11-09 삼성전자주식회사 Cathode material for fuel cell, cathode for fuel cell and solid oxide fuel cell including the material
WO2015106769A1 (en) * 2014-01-14 2015-07-23 Elcogen As A method of producing sofc cathode diffusion barrier layer and a sofc

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070009784A1 (en) 2005-06-29 2007-01-11 Pal Uday B Materials system for intermediate-temperature SOFC based on doped lanthanum-gallate electrolyte
JP2008257943A (en) * 2007-04-03 2008-10-23 Mie Univ Electrode for solid oxide fuel cell and solid oxide fuel cell having the electrode
EP2254180A1 (en) 2007-08-31 2010-11-24 Technical University of Denmark Ceria and strontium titanate based electrodes
JP5454434B2 (en) * 2009-09-30 2014-03-26 大日本印刷株式会社 Single-chamber solid oxide fuel cell
CN103155255B (en) 2010-08-17 2015-09-30 博隆能源股份有限公司 The manufacture method of solid-oxide fuel cell
GB201019156D0 (en) * 2010-11-12 2010-12-29 Ulive Entpr Ltd Mixed metal oxide
EP2506351A3 (en) 2011-03-31 2014-11-12 Samsung Electro-Mechanics Co., Ltd Material for solid oxide fuel cell, cathode including the material, and solid oxide fuel cell including the same
US10446855B2 (en) * 2013-03-15 2019-10-15 Lg Fuel Cell Systems Inc. Fuel cell system including multilayer interconnect
JP6121764B2 (en) * 2013-03-22 2017-04-26 日本碍子株式会社 Air electrode used in solid oxide fuel cell
JP6100050B2 (en) * 2013-03-25 2017-03-22 日本碍子株式会社 Air electrode for fuel cell
JP2015076129A (en) * 2013-10-04 2015-04-20 日産自動車株式会社 Air electrode material for fuel cell, air electrode for fuel cell and solid oxide fuel cell
JP2015185321A (en) * 2014-03-24 2015-10-22 アイシン精機株式会社 Air electrode for solid oxide fuel batteries, and solid oxide fuel battery cell
JP6315581B2 (en) * 2014-08-22 2018-04-25 国立大学法人 熊本大学 Cathode for solid oxide fuel cell, method for producing the same, and solid oxide fuel cell including the cathode

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010232135A (en) * 2009-03-30 2010-10-14 Mitsubishi Materials Corp Durable fuel electrode and solid oxide fuel cell incorporating this fuel electrode
US20120064433A1 (en) * 2010-09-14 2012-03-15 Samsung Electro-Mechanics Co., Ltd. Material for solid oxide fuel cell, cathode including the material, and solid oxide fuel cell including the material
KR20120123639A (en) * 2011-04-19 2012-11-09 삼성전자주식회사 Cathode material for fuel cell, cathode for fuel cell and solid oxide fuel cell including the material
WO2015106769A1 (en) * 2014-01-14 2015-07-23 Elcogen As A method of producing sofc cathode diffusion barrier layer and a sofc

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
D. PEREZ-COLL ET AL.: "Optimization of the interface polarization of the La Ni0 -based cathode working with the Ce . Sm 0 -[delta] electrolyte system", JOURNAL OF POWER SOURCES, vol. 178, no. 1, pages 151 - 162
KEQIN HUANG ET AL.: "Increasing Power Density of LSGM-Based Solid Oxide Fuel Cells Using New Anode Materials", JOURNAL OF THE ELECTROCHEMICAL SOCIETY, vol. 148, no. 7, pages A788, XP055633789, DOI: 10.1149/1.1378289
PEREZ-COLL ET AL., OPTIMIZATION OF THE INTERFACE POLARIZATION OF THE LA NI0 -BASED CATHODE WORKING WITH THE CE ,S ,0 ELECTROLYTE SYSTEM
See also references of EP3465807A4
ZHAO, HUI ET AL.: "Ln2M04 cathode materials for solid oxide fuel cells", SCIENCE CHINA CHEMISTRY, vol. 54, no. 6, 2011, pages 898 - 910, XP19909978 *

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