Solid oxide fuel cells (SOFCs) have gained significant interest due to their high energy conversion efficiency, low pollution emission, and high fuel flexibility. Recent research on SOFCs is aimed at reducing the operating temperature to 650-850° C. This will enable the use of oxidation resistant alloys in place of the traditional ceramic interconnect materials used in high-temperature (˜1000° C.) SOFC stacks [1-9]. The metallic interconnects have many advantages including low materials cost, excellent mechanical properties, high thermal conductivity and easy manufacturing processing that is scalable to large areas. However, their lifetime is limited by the conductivity of the oxide scale, typically Cr2O3, (chromia), that forms on the surface. Chromia is electrically insulating, leading to higher contact resistance, which is deleterious to the fuel cell performance. In addition, volatile Cr species can be released from the Cr2O3 scale, depending on the temperature and partial pressures of H2O and O2 [10]. The presence of the volatile chromium species, notably CrO2(OH)2, in the cathode of an SOFC is known to cause rapid poisoning of the cathode and/or the cathode/electrolyte interface, and performance degradation [11].
The interconnection is a vital component in a fuel cell stack and connects the anode of a cell to the cathode of the adjacent cell. It is subjected to harsh environments at high temperatures in the range of 600-800° C., i.e., very oxidizing conditions on the cathodic side and very reducing conditions on the anodic side. Chromium and nickel based alloys are presently used as the interconnection materials, but they form poorly conducting oxidic scales under these conditions, especially on the cathodic side. Previously proposed protective coating layers include coatings of conductive perovskite compositions, such as Sr-doped lanthanum manganite, ferrite and chromite, which are often used as cathode and interconnect materials in SOFCs [6,13]. Protective spinel coatings also have been investigated. Previous work on spinel layers on stainless steel indicated that a (Mn,Co)3O4 spinel coating layer could be a promising barrier to chromium migration [14-16]. Copper-manganese spinels exhibit high electrical conductivity and a matching coefficient of thermal expansion at fuel cell operating temperatures [17,18].
Thus, a need exists for oxide film compositions that are electrically conductive and also suppress the rate of oxide layer growth.
The invention provides an electrically conductive protective coating produced by electrophoretic deposition on a ferritic alloy, such as stainless steel. The coating comprises a spinel compound, such Cu(x)Mn(y)O(z), wherein x=1, 1.6≦y≦2.4, and z=4. In a preferred embodiment the protective coating contains CuMn1.8O4.
Another aspect of the invention is an electrical interconnect device for a solid oxide fuel cell. The interconnect device includes a stainless steel substrate and a protective oxide coating deposited on the substrate. The protective coating contains Cu(x)Mn(y)O(z), wherein x=1, 1.6≦y≦2.4, and z=4. In a preferred embodiment the protective coating contains CuMn1.8O4, and the stainless steel substrate is Crofer 22 APU.
Yet another aspect of the invention is a method of depositing an electrically conductive protective coating onto a ferritic alloy. The method includes providing a ferritic alloy substrate immersed in a liquid suspension of a spinel compound. In a preferred embodiment, the spinel compound has the formula Cu(x)Mn(y)O(z), wherein x=1, 1.6≦y≦2.4, and z=4. The spinel compound is electrophoretically deposited onto the substrate by applying a DC voltage between the substrate and an electrode immersed in the liquid suspension. The resulting coated substrate can be used as a solid oxide fuel cell interconnect.
Other features and advantages of the invention will be apparent from the following description of the preferred embodiments thereof and from the claims, taken in conjunction with the accompanying drawings, in which:
U.S. Provisional Application entitled PROTECTIVE OXIDE COATINGS FOR SOFC INTERCONNECTIONS, filed on Aug. 2, 2007 and having Ser. No. 60/963,042, is hereby incorporated by reference in its entirety.
The present invention provides a protective oxide coating applied on metallic alloys used as interconnect materials for solid oxide fuel cells. The coating is applied using an electrophoretic deposition technique and has been shown to significantly suppress the kinetics of oxide layer formation, thus extending the life of the interconnection material and the fuel cell stack. This invention also makes possible the use of less expensive stainless steels as solid oxide fuel cell interconnects, thereby reducing the overall stack cost. The protective oxide coating of the invention is also expected to suppress chromium diffusion into the cathode.
Referring to
A protective oxide coating according to the invention is a spinel coating that has been applied by electrophoretic deposition (EPD). A spinel is a mineral composition of the general formula AB2O4, where A and B can be divalent, trivalent, or quadrivalent cations, including magnesium, zinc, iron, manganese, copper, aluminum, chromium, titanium, and silicon. In a preferred embodiment, the spinel coating has a composition corresponding to Cu(x)Mn(y)O(z), where x=1, 1.6≦y≦2.4, and z=4. More preferably, the spinel coating has a composition corresponding to Cu(x)Mn(y)O(z), where x=1, 1.8≦y≦2.0, and z=4. In a preferred embodiment, the spinel coating has the formula CuMn1.8O4. Other variations in the composition family Cu(x)Mn(y)O(z) may also be used, such as where x=1, z=4, and y=1.7, 1.9, 2.1, 2.2, or 2.3. Examples of other spinel compounds suitable for use in a protective oxide coating of the invention include MnCo2O4, Mn1.5Co1.5O4, LaCrO3, NiCrO3, La0.8Sr0.2MnO3, La0.8Sr0.2CrO3, La0.8Sr0.2FeO3, La0.67Sr0.33MnO3, (La0.8Sr0.15)0.9MnO3, La0.9Sr0.1CrO3, La0.6Sr0.4CoO3, La0.6Sr0.4CrO3, and YxCa1-xMnO3 (where 0.1<x<0.4).
The coating can be deposited on the surface of an alloy being used as the interconnect using a range of deposition techniques. A preferred deposition technique is electrophoretic deposition (EDP). Other deposition techniques like thermal spraying, screen printing followed by sintering, air spraying followed by sintering, or sputtering also can be used to deposit a protective spinel layer, such as a spinel compound corresponding to Cu(x)Mn(y)O(z), where x=1, 1.6≦y≦2.4, and z=4.
A protective coating layer applied to an SOFC interconnect is intended to serve as a barrier to prevent chromium migration from the chromium-containing metal substrate, while minimizing the contribution of the interfacial contact to the area specific resistance between the cathode and the interconnect [12].
A ferritic alloy that serves as a substrate for deposition of a protective oxide coating according to the invention can be any ferritic alloy, such as a stainless steel. For use as an SOFC interconnect, the ferritic alloy is preferably resistant to oxidation, stable at high temperatures on the order of 800° C., and has a thermal expansion coefficient similar to that of other materials in the SOFC stack. Preferably, the ferritic alloy is a ferritic stainless steel such as a 400 series stainless steel, such as stainless steel types 430, 444, and 446. Especially preferred are Crofer 22 APU (UNS S44535), manufactured by ThyssenKrupp VDM GmbH (Germany), ZMG232, manufactured by Hitachi Metals Co., Ltd (Japan); and Ebrite (UNS 44627) manufactured by Allegheny Ludlum Corp. (USA); these are high temperature alloys especially designed for use as SOFC interconnects.
A substrate for use with a protective oxide coating or a method of the invention can have any shape or geometry required for its subsequent use after the protective coating is applied. For example, if the coated substrate is intended for use as an SOFC interconnect, it can have any form consistent with such application, including a flat plate, a plate with channels on one or both sides for electrolyte solution, fuel, or oxidant, or any form required by a given fuel cell stack geometry.
Any application requiring oxidation protection of ferritic alloys can in principle employ a protective coating according to the invention. In particular, a protective oxide layer according to the invention can be used in any application requiring corrosion resistance and simultaneously maintenance of an electrically conductive surface. For example, the coatings and methods of the invention can be used to prepare components of machinery or electronics that may be exposed to extreme conditions, such as high heat, and require an electrically conductive surface, resistance to oxidation, or resistance to migration of elements such as Cr out of the substrate.
A number of approaches can be used for applying protective layers on interconnect and coating materials. These include, e.g., plasma-spraying [19], electron-beam physical vapor deposition (EB-PVD) [20], and RF-magnetron sputtering [21]. However, these processes are generally expensive due to high capital equipment cost. In contrast, colloidal deposition routes are simple and inexpensive methods, and have been used, for example, to process advanced ceramics [22]. The electrophoretic deposition method (EPD) is a colloidal fabrication process in which charged particles dispersed in a liquid medium are attracted and deposited onto conductive and oppositely charged electrodes upon application of a DC electric field. EPC has the advantages of short deposition time, little restriction in the shape of substrates, simple deposition apparatus, and easy scalability for mass production. In particular, EPD offers easy control of the thickness and morphology of the deposited film through simple adjustment of the deposition time and applied potential [23]. For example, to increase film thickness, either the electric field strength can be increased, or the time of electrophoretic deposition can be increased, or both. Aqueous suspensions are used most often, but organic suspensions also can be used [24-25].
According to a method of the invention, a thin, dense, conductive spinel coating is deposited on a substrate containing or made entirely from a ferritic alloy, such as a ferritic stainless steel, using an EPD method. A flow chart for a coating procedure according to the invention is shown in
The spinel coated can be deposited onto the substrate by establishing a constant voltage between the ferritic alloy substrate as the cathode and another electrode (the anode) placed in the spinel suspension, e.g., about 1.5 cm removed from the substrate. A voltage in the range from about 1 to about 200 V, preferably from about 1 to about 50 V, can be used; more preferably the voltage is about 20V. EPD is carried out for a time from about 0.1 min to about 100 min, preferably from about 5 to about 100 min, more preferably from about 5 to about 30 min, such as, for example, about 10 min. The voltage and time should be selected to provide the desired coating thickness, while maintaining a uniformly thick and dense coating, preferably avoiding conditions that might leave thin or bare zones that locally could reduce the corrosion resistance of the coating. Generally, a thickness in the range from about 1 μm to about 500 μm can be used.
Following the EPD step, the coating optionally is subjected to mechanical pressure followed by annealing at high temperature. Annealing should be performed at a temperature of at least 500° C. for a period of at least 1 hour. For example, the coating can be annealed at 850° C. for two hours. Following annealing, further optional steps include mechanical pressure and sintering at high temperature in air for an extended period of time (e.g., 800° C. for 100 h).
The following examples are presented to illustrate the advantages of the present invention and to assist one of ordinary skill in making and using the same. These examples are not intended in any way otherwise to limit the scope of the disclosure.
A commercial ferritic stainless steel, Crofer 22 APU, with a chemical composition (in wt. %) of 22.8 Cr, 0.45 Mn, 0.08 Ti, 0.06 La, 0.005 C, ≦0.03 P, ≦0.03 S, balance Fe, was used as the substrate for the coating. Crofer 22 APU substrates of dimensions 25 mm×20 mm×0.5 mm were mechanically polished with various grades of SiC paper, up to 1200 grit. Prior to film deposition, the substrates were ultrasonically cleaned in acetone.
Powders of nominal composition CuMn1.8O4 were prepared by the solid-state reaction method. Proportional amounts of precursors CuO (99.99%) and Mn2O3 (99.9%) were thoroughly mixed and calcined at 1000° C. The calcined powders were crushed and ball-milled, after which the procedure was repeated. The average grain size of the powder used in this experiment was about 0.1 μm. The suspensions of CuMn1.804 spinel used in this study were prepared by mixing the spinel powder in acetone/ethanol (3/1 volume ratio) mixture with iodine. The concentration of CuMn1.8O4 in the suspension was maintained constant at 1.2 g/L. Before EPD of CuMn1.8O4 particles, the suspensions were dispersed ultrasonically for 20 min and then were allowed to settle for 10 minutes. Electrophoretic deposition experiments were carried out at a constant voltage 20 V for 10 min. After deposition, the coating was mechanically pressed and sintered at 800° C. for 100 h.
The coatings produced in Example 1 were characterized by X-ray diffraction (XRD) using a Bruker D8 Advance XRD system with Cu Kα radiation. The morphology of the coating was analyzed using scanning electron microscopy (SEM). The oxidation was continuously monitored by thermogravimetry using a TA Q600 thermobalance.
The cross-sectional view of CuMn1.8O4 spinel coating on Crofer 22 APU substrate sintered at 800° C. for 100 hours is shown in
The results of an oxidation study for the CuMn1.8O4-coated Crofer 22 substrates of Example 1 are shown in
Elemental distribution analysis was performed by SEM/EDX (SEM energy dispersive X-ray analysis).
The effect of a protective coating according to the invention on the thermal oxidation of a ferritic steel substrate was estimated. Based on the data previously discussed, the structures of coated and uncoated Crofer 22 APU after thermal oxidation can be schematically displayed as in
where x is the oxide thickness, and t is time. The buildup of the oxide scale over time is due to the oxygen concentration difference between the oxide/alloy interface and the oxide/air surface. Thus, it is reasonable to assume that
where K is a constant representing the effective diffusion coefficient. According to Wagner's theory of oxidation,
where kp is the parabolic rate constant. Then
Integration of equation (1) through the thickness of the oxide layer yields
where R is the gas constant, T is temperature, pO2(air) is 0.21 atm and pO2(Cr2O3/alloy) is 1.5×10−28 atm, which is close to the known thermodynamic equilibrium oxygen partial pressure for the coexistence of Cr+Cr2O3. According to previous data, kp of uncoated and coated Crofer 22 APU at 800° C. are around 10.51×10−2 and 2.87×10−2 μm h−1/2. Thus, the K value for uncoated and coated Crofer 22 APU can be estimated as 4.46×103 and 1.22×103, respectively. The K value for uncoated Crofer 22 APU is essentially the effective diffusion coefficient of MnCr2O4 and Cr2O3 mixed layer. And the K for coated Crofer 22 APU is essentially the combined effective diffusion coefficient of the spinel coating layer and the MnCr2O4 and Cr2O3 mixed oxide scale.
For a two-layer system, the K value of each layer can be treated as serial resistances. Thus, they will have the following relationship.
Here, δ1 and δ2 are the thicknesses of the coating and oxides, respectively. δ1+δ2 is the total thickness of the coating and the oxides. Kcoating and Koxides are the effective diffusion coefficient of the coating and oxides, respectively. Kcombined is the combined effective diffusion coefficient of the coating and the oxides. As shown in
The area specific resistance of uncoated and CuMn1.8O4-coated Crofer 22 APU substrates was investigated. Area specific resistance (ASR) was measured according to Huang [27]. The resistivity of the substrate was assumed to be negligible compared with that of the thermally grown scale or electrophoretically deposited coating on the surface of the alloy substrate. Thus, the measured ASR includes that of the scale or scale+coating layer and its interface with the substrate and the Pt electrode. Since the current used (0.1 A) was relatively small, interfacial polarization was negligible. The measured ASR was therefore assumed to be that of the scale or scale+coating layer.
The results shown in
Using calculations according to Example 5, and assuming a parabolic increase over time of a Cr2O3 oxide layer under a CuMn1.8O4 spinel coating on a Crofer 22 APU substrate, the oxide thickness formed after 50,000 hours at 800° C. is estimated to be 6.4 μm. Given an electrical resistivity for Cr2O3 at 800° C. of about 18 Ω·cm [28], the ASR of a CuMn1.8O4 spinel coating on a Crofer 22 APU substrate is expected to provide an acceptable value of less than 0.1 Ω·cm2 for SOFC interconnect materials over their expected service lifetime.
While the present invention has been described in conjunction with one or more preferred embodiments, one of ordinary skill, after reading the foregoing specification, will be able to effect various changes, substitutions of equivalents, and other alterations to the compositions and methods set forth herein. It is therefore intended that the protection granted by Letters Patent hereon be limited only by the definitions contained in the appended claims and equivalents thereof.
This application claims priority to U.S. Provisional Application entitled PROTECTIVE OXIDE COATINGS FOR SOFC INTERCONNECTIONS filed on Aug. 2, 2007 and having Ser. No. 60/963,042, which is incorporated by reference herein.
Number | Date | Country | |
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60963042 | Aug 2007 | US |