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Low Temperature Electrolytes for Solid Oxide Cells Having High Ionic Conductivity

Inactive Publication Date: 2013-06-13
FCET
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The present invention provides a method to enhance the conductivity of ionic metal oxides in solid oxide cells, which allows for lower operating temperatures. This results in the use of simpler and less expensive materials in the construction of the cells, leading to lower production costs. The lower operating temperatures also allow for higher strength in metal components, allowing for higher levels of porosity. Additionally, the invention reduces degradation processes associated with variances in coefficients of thermal expansion between components of the cell. Finally, the invention produces a desirable surface catalytic effect, resulting in more chemically active sites at triple phase boundaries for more efficient fuel cell operation.

Problems solved by technology

The need for exotic materials greatly increases the costs of solid oxide fuel cells, making their use in certain applications cost-prohibitive.
Significantly, the high operating temperature is required because of poor low temperature ion conductivity.
However, high proton conductivity requires precise control of hydration in the electrolyte.
If the electrolyte becomes too dry, proton conductivity and cell voltage drop.
If the electrolyte becomes too wet, the cell becomes flooded.
Electro-osmotic drag complicates hydration control: protons migrating across the electrolyte “drag” water molecules along, potentially causing dramatic differences in hydration across the electrolyte that inhibit cell operation.
In conventional electrolyzers, electrical energy is lost in the electrolysis reaction driving the diffusion of ions through the electrolyte and across the distance between the electrodes.
However, at higher temperatures, electrolyzers face similar thermal stresses and cracking caused by differences in coefficients of thermal expansion between components of the solid oxide electrolyzer cell.
Moreover, given the high operating temperature of lambda sensors and similar devices, sensors face thermal stresses, cracking, and delamination issues similar to those facing fuel cells and electrolyzers.
Moreover, the efficiency losses due to the thickness of electrolytes make thinner electrolytes desirable.
Incorporating higher porosity levels in ceramic materials renders them too structurally weak to support cell construction.
High sintering temperatures during fabrication of various components, such as the electrolyte, can compound problems associated with variances in coefficients of thermal expansion.

Method used

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  • Low Temperature Electrolytes for Solid Oxide Cells Having High Ionic Conductivity
  • Low Temperature Electrolytes for Solid Oxide Cells Having High Ionic Conductivity
  • Low Temperature Electrolytes for Solid Oxide Cells Having High Ionic Conductivity

Examples

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example 1

[0213]FIG. 3 depicts one embodiment of the invention in the form of a solid oxide cell having a metal oxide electrolyte 380 positioned between a first electrode 310 and a second electrode 320. The metal oxide electrolyte 380 comprises a powder 350 together with a metal oxide 360. In some cases, the powder 350 can be mixed with one or more metal compounds to form a slurry that is then applied by spin coating, brushing, or other suitable method onto the first electrode 310 (or second electrode 320). Then, the metal compound is converted to form the metal oxide 360, for example, by heating the atmosphere about the metal compound, or by inductively heating the first electrode 310. Optionally, once a layer of the metal oxide electrolyte 380 has been formed, additional powder-metal compound slurry can be applied and heated to form a thicker metal oxide electrolyte 380. The cell is assembled by placing the second electrode 320 onto the metal oxide electrolyte 380, or, optionally, additiona...

example 2

[0215]FIG. 4 depicts another embodiment of the present invention, in which a first metal oxide 450 and a second metal oxide 460, disposed in interpenetrating domains of metal oxides, form a metal oxide electrolyte between two electrodes 410, 420. To form such domains, a first metal compound composition is applied to the first electrode 410 and converted to a first metal oxide 450, such as, for example, strontium titanate. Then, a second metal compound composition is applied to the first metal oxide 450 and allowed to accumulate in pores, imperfections, and defects in the first metal oxide so formed. The second metal oxide composition is converted to form a second metal oxide 460, such as, for example, yttria-stabilized zirconia. Six alternating layers of the first metal oxide 450 and the second metal oxide 460 are formed in this embodiment.

[0216]In operation, for example, air or other oxygen-containing gas is supplied to the first electrode 410, which acts as the cathode to reduce d...

example 3

[0217]FIG. 5 depicts a solid oxide cell according to one embodiment of the present invention. A nanobar 540 and a metal oxide 560, disposed so that the nanobars 540 orient substantially perpendicularly to a first planar electrode 510, form a metal oxide electrolyte 580 between two electrodes 510, 520. The nanobar 540 can be, for example, a multi-walled carbon nanotube of semiconductor characteristic, oriented in metal oxide 560 which can be, for example, yttria-stabilized zirconia. To make the cell of FIG. 5, chosen nanobars 540 are combined with at least one metal compound in a metal compound composition, that is then applied to the first electrode 510. An orienting force is then applied. Optionally, the first electrode with the metal compound composition is placed in a magnetic field, at least a portion of the nanobars orient due to the magnetic field, and the metal compound composition is converted to form the metal oxide 560. Or, an electric field is applied to orient at least a...

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Abstract

Some embodiments of the present invention provide solid oxide cells and components thereof having a metal oxide electrolyte that exhibits enhanced ionic conductivity. Certain of those embodiments have two materials, at least one of which is a metal oxide, disposed so that at least some interfaces between the domains of the materials orient in a direction substantially parallel to the desired ionic conductivity.

Description

CROSS REFERENCE TO RELATED APPLICATIONS[0001]The present application claims benefit of priority under PCT Article 8 and 35 U.S.C. §119(e) of U.S. Provisional Application No. 61 / 303,003, filed on Feb. 10, 2010, entitled, “LOW TEMPERATURE ELECTROLYTES FOR SOLID OXIDE CELLS HAVING HIGH IONIC CONDUCTIVITY.” That provisional application is incorporated herein by reference in its entirety.STATEMENT REGARDING FEDERALLY-SPONSORED RESEARCH AND DEVELOPMENT[0002]This invention was made with government support awarded by the Department of Energy and administered by Oak Ridge National Laboratory / UT Battelle. The government has certain rights in the invention.FIELD OF THE INVENTION[0003]The present invention relates to electrical energy systems such as fuel cells, electrolyzer cells, and sensors, and, in particular, to solid oxide fuel cells, solid oxide electrolyzer cells, solid oxide sensors, and components of any of the foregoing.BACKGROUND OF THE INVENTION[0004]Solid oxide fuel cells, otherwi...

Claims

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Application Information

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IPC IPC(8): H01M8/12C25B9/00C25B5/00G01N27/28C25B9/19C25B9/23
CPCH01B1/122H01M2300/0091C25B9/00G01N27/28H01M8/1246C25B9/10H01M8/1253H01M8/126Y02E60/521Y02E60/525H01M8/243H01M2008/1293H01M2300/0074H01M2300/0077C25B5/00C25B13/04Y02E60/50Y02P70/50C25B9/19C25B9/23H01M8/0271C04B35/628H01M8/1007G01N27/40G01N27/4073H01M8/004H01M8/1006H01M8/1016H01M2300/0071
Inventor BUDARAGIN, LEONID V.DEININGER, MARK A.POZVONKOV, MICHAEL M.SPEARS, II, D. MORGANFISHER, PAUL D.LUDTKA, GERARD M.PASTO, ARVID E.
Owner FCET
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