Patent Application
20130236813
This application claims priority to and the benefit of Korean Patent Application No. 10-2012-0024452, filed on Mar. 9, 2012, and all the benefits accruing therefrom under 35 U.S.C. §119, the content of which is incorporated herein in its entirety by reference.
1. Field
The present disclosure relates to an inorganic ion conductor, a method of forming the inorganic ion conductor, and a fuel cell including the inorganic ion conductor.
2. Description of the Related Art
Fuel cells can be classified as a polymer electrolyte membrane fuel cell (PEMFC), a direct methanol fuel cell (DMFC), a phosphoric acid fuel cell (PAFC), a molten carbonate fuel cell (MCFC), or a solid oxide fuel cell (SOFC) depending on the type of electrolyte and the fuel used.
SOFCs can be suitable for use as a decentralized power supply, due to their high electrical efficiency and operability with a variety of fuels, including lower purity gaseous fuels. However, to provide for operation at high temperatures, SOFCs use more costly materials which are durable in high-temperature environments. Also, it is not easy to rapidly switch a SOFC on or off because of the heating or cooling time. Thus SOFCs are less suitable for portable power or vehicular power sources where rapid startup and shutdown are desirable. Therefore, research to provide a SOFC which can operate at a lower temperature is being actively conducted.
PEMFCs operating at 100° C. or higher in non-humidified conditions, as compared to those operating at low temperatures, do not need a humidifier, and are known to be convenient in terms of control of water supply and highly reliable in terms of system operation. Furthermore, such PEMFCs may become more durable against carbon monoxide (CO) poisoning that may occur at fuel electrodes as they operate at high temperatures, and thus, a simplified reformer may be used therefor. These advantages mean that PEMFCs are increasingly drawing attention for use in such high-temperature, non-humidifying systems.
Along with the current trends of lowering the operation temperature of SOFCs and increasing the operation temperature of PEMPCs as described above, fuel cells operable in a moderate temperature range are drawing more attention.
However, electrolyte membranes of fuel cells that have been developed so far do not exhibit satisfactory conductivity at moderate temperatures, and thus, there remains a need for an improved electrolyte material.
Provided is an inorganic ion conductor having suitable conductivity, a method of forming the inorganic ion conductor, and a fuel cell including the inorganic ion conductor and having improved efficiency.
Additional aspects will be set forth in part in the description which follows and, in part, will be apparent from the description.
According to an aspect, an inorganic ion conductor including a trivalent metallic element, a pentavalent metallic element, phosphorus (P); and oxygen (O) is provided.
According to another aspect, an inorganic ion conductor represented by Formula 1 below is provided:
A0.5-xQ0.5-yP2O7, Formula 1
wherein A is a trivalent metallic element, Q is a pentavalent metallic element, x is 0 to about 0.45, and y is 0 to about 0.45.
According to another aspect, a method of forming an inorganic ion conductor includes contacting a trivalent metal precursor, a pentavalent metal precursor, and a phosphoric acid precursor to obtain a mixture; and thermally treating the mixture to form the inorganic ion conductor, wherein the inorganic ion conductor includes the trivalent metallic element, the pentavalent metallic element, phosphorus (P), and oxygen (O).
According to another aspect, a method of forming an inorganic ion conductor includes contacting a trivalent metal precursor, a pentavalent metal precursor, and a phosphorous precursor to obtain a mixture; and thermally treating the mixture to obtain an inorganic ion conductor represented by Formula 1:
A0.5-xQ0.5-yP2O7, Formula 1
wherein A is a trivalent metallic element, Q is a pentavalent metallic element, x is 0 to about 0.45, and y is 0 to about 0.45.
Also provided is an electrode for a fuel cell including the inorganic ion conductor disclosed above.
Also provided is a fuel cell including the inorganic ion conductor described above.
An electrolyte for a fuel cell includes the inorganic ion conductor described above.
A fuel cell including the inorganic ion conductor described above is provided.
An electrochemical device including the inorganic ion conductor described above is also provided.
These and/or other aspects will become apparent and more readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings in which:
Reference will now be made in detail to embodiments, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to like elements throughout. In this regard, the present embodiments may have different forms and should not be construed as being limited to the descriptions set forth herein. Accordingly, the embodiments are merely described below, by referring to the figures, to explain aspects of the present description.
It will be understood that when an element is referred to as being “on” another element, it can be directly on the other element or intervening elements may be present therebetween. In contrast, when an element is referred to as being “directly on” another element, there are no intervening elements present.
It will be understood that, although the terms “first,” “second,” “third” etc. may be used herein to describe various elements, components, regions, layers, and/or sections, these elements, components, regions, layers, and/or sections should not be limited by these terms. These terms are only used to distinguish one element, component, region, layer, or section from another element, component, region, layer, or section. Thus, “a first element,” “component,” “region,” “layer,” or “section” discussed below could be termed a second element, component, region, layer, or section without departing from the teachings herein.
The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting. As used herein, the singular forms “a,” “an,” and “the” are intended to include the plural forms, including “at least one,” unless the content clearly indicates otherwise. “Or” means “and/or.” As used herein, the term “and/or” includes any and all combinations of one or more of the associated listed items. It will be further understood that the terms “comprises” and/or “comprising,” or “includes” and/or “including” when used in this specification, specify the presence of stated features, regions, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, regions, integers, steps, operations, elements, components, and/or groups thereof.
Spatially relative terms, such as “beneath,” “below,” “lower,” “above,” “upper” and the like, may be used herein for ease of description to describe one element or feature's relationship to another element(s) or feature(s) as illustrated in the figures. It will be understood that the spatially relative terms are intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, elements described as “below” or “beneath” other elements or features would then be oriented “above” the other elements or features. Thus, the exemplary term “below” can encompass both an orientation of above and below. The device may be otherwise oriented (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.
Unless otherwise defined, all terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this disclosure belongs. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and the present disclosure, and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein.
Exemplary embodiments are described herein with reference to cross section illustrations that are schematic illustrations of idealized embodiments. As such, variations from the shapes of the illustrations as a result, for example, of manufacturing techniques and/or tolerances, are to be expected. Thus, embodiments described herein should not be construed as limited to the particular shapes of regions as illustrated herein but are to include deviations in shapes that result, for example, from manufacturing. For example, a region illustrated or described as flat may, typically, have rough and/or nonlinear features. Moreover, sharp angles that are illustrated may be rounded. Thus, the regions illustrated in the figures are schematic in nature and their shapes are not intended to illustrate the precise shape of a region and are not intended to limit the scope of the present claims.
According to an embodiment, an inorganic ion conductor including a trivalent metallic element, a pentavalent metallic element, phosphorus (P), and oxygen (O) is provided.
The trivalent metallic element is a metallic element having an oxidation number of 3, and it is at least one selected from aluminum (Al), iron (Fe), gallium (Ga), yttrium (Y), indium (In), antimony (Sb), bismuth (Bi), lanthanum (La), neodymium (Nd), and samarium (Sm). In and Fe are specifically mentioned. Also, the pentavalent metallic element is a metallic element having an oxidation number of 5, and it is at least one selected from antimony (Sb), niobium (Nb), bismuth (Bi), vanadium (V), and tantalum (Ta). Sb, Nb, and Ta are specifically mentioned.
The inorganic ion conductor including P and O may comprise at least one selected from an orthophosphate, and a pyrophosphate, and the like. Particularly, for the inorganic ion conductor, for example, a pyrophosphate including a trivalent metallic element and a pentavalent metallic element is specifically mentioned.
A pyrophosphate refers to a compound having an ion represented by Formula 2:
The inorganic ion conductor may have a cubic or pseudo-cubic crystal structure. Here, the term “pseudo-cubic” refers to a rhombohedral structure, which is similar to a cubic structure. The pseudo-cubic, e.g., rhombohedral structure, crystal structure may be confirmed by analyzing a distance between lattice planes of the crystal obtained in an X-ray diffraction analysis.
While not wanting to be bound by theory, it is understood that the inorganic ion conductor may have a structure in which metal oxide octahedra (e.g., a metal oxide octahedron of the formula MO6) are located at each corner and at each center of the cubic faces of the structure to provide a face-centered cubic structure. Also, a phosphate group (e.g., a group of the formula P2O7) may be located at each of edges of the structure, and the phosphate groups may bind the metal oxide octahedra.
The crystal structure may be identical to or similar to, e.g., isostructural with, a crystalline phase of, for example, a compound of the formula MP2O7, wherein M refers to a tetravalent metallic element. M may be, for example, at least one selected from tin (Sn), zirconium (Zr), and titanium (Ti).
The inorganic ion conductor may be an inorganic ion conductor including a compound represented by Formula 1:
A0.5-xQ0.5-yP2O7, Formula 1
In Formula 1, A is a trivalent metallic element, Q is a pentavalent metallic element, x is 0 to about 0.45, and y is 0 to about 0.45.
According to an embodiment, x is 0 to about 0.2, and y is 0 to about 0.2. In another embodiment, x is about 0.1 to about 0.4, and y is about 0.1 to about 0.4.
In Formula 1, the trivalent metallic element is at least one selected from aluminum (Al), iron (Fe), gallium (Ga), yttrium (Y), indium (In), antimony (Sb), bismuth (Bi), lanthanum (La), neodymium (Nd), and samarium (Sm). Also, the pentavalent metallic element is at least one selected from antimony (Sb), niobium (Nb), bismuth (Bi), vanadium (V), and tantalum (Ta).
The inorganic ion conductor may be synthesized in a form of, for example, AIII0.5-xBV0.5P2O7 or AIII0.5BV0.5-yP2O7, wherein x is 0 to about 0.45 and y is 0 to about 0.45. Also, cation defects may be generated due to charge compensation of the trivalent or the pentavalent metallic element, and thus a proton may be dissolved in the conductor by a reaction with water vapor. As a result, ionic conductivity of the inorganic ion conductor is improved.
Moreover, as shown in Formula 1, the inorganic ion conductor has a structure in which a content of the trivalent and pentavalent metallic elements compared to a content of P and O may not satisfy a stoichiometric composition. Due to such structure, more lattice defects in the compound may be generated than in a compound in which a content of P and O satisfies a stoichiometric composition, such as Sn0.9In0.1P2O7. Thus a concentration of protons that may be introduced in the compound is increased, thereby improving ionic conductivity of the inorganic ion conductor.
In an embodiment the inorganic ion conductor may have peak conductivity in different temperature regions depending on a type of the pentavalent metallic element. Thus, an inorganic ion conductor having excellent ionic conductivity at various temperature ranges may be provided by selecting a type of the pentavalent metallic element. For example, the inorganic ion conductor may provide a conductor that is suitable for use at a plurality of temperature zones within a temperature range of about 100° C. to about 400° C. For example, if the pentavalent metallic element is Ta, the inorganic ion conductor may have high ionic conductivity at a temperature of 200° C. to 400° C. Also, if the pentavalent metallic element is Sb or Nb, the inorganic ion conductor may have excellent ionic conductivity at a lower temperature, e.g., 100° C. to 200° C. The conductivity of the inorganic ion conductor, when measured between about 10 to about 106 Hz and using an AC having an amplitude of 10 mV, may be greater than about 0.025 Siemens per centimeter (Scm−1), specifically greater than about 0.04 Scm−1, more specifically greater than about 0.06 Scm−1 at 100° C. The conductivity of the inorganic ion conductor, when measured between about 10 to about 106 Hz and using an AC having an amplitude of 10 mV, may be greater than about 0.05 Siemens per centimeter (Scm−1), specifically greater than about 0.06 Scm−1, more specifically greater than about 0.1 Scm−1 at 200° C.
The inorganic ion conductor may have a crystal structure which is identical to or similar to, e.g., isostructural with, a crystalline phase of the formula MP2O7 (wherein M is a tetravalent metallic element, for example, at least one selected from Sn, Zr, and Ti) as described above, and if the inorganic ion conductor has such crystal structure, the inorganic ion conductor provides excellent conductivity.
The crystalline phase of the pyrophosphate of the formula MP2O7 may have a peak of greatest intensity in a range of about 15 degrees to about 25 degrees two-theta (a Bragg angle, 2θ), when analyzed by X-ray diffraction with CuK-α X-ray radiation having wavelength of 1.541 Angstroms (Å). Here, the peak of greatest intensity refers to a diffraction peak that has an intensity greater than any other peak between 5 and 80 degrees 2θ.
The inorganic ion conductor may have excellent conductivity if the peak of greatest intensity in a range of about 15 degrees to about 25 degrees, when analyzed using CuK-α X-ray radiation having wavelength of 1.541 Å, appears in a region corresponding to a crystalline phase of SnP2O7. An example of such an inorganic ion conductor may be Fe0.5Ta0.5P2O7, Fe0.5Nb0.5P2O7, or In0.5Sb0.5P2O7. A combination comprising at least one of the foregoing can be used.
The region corresponding to the crystalline phase of SnP2O7 is in a range of about 15 degrees to about 25 degrees 2θ and/or in a range of about 30 degrees to about 40 degrees 2θ, and a peak of greatest intensity is in a range of about 15 degrees to about 25 degrees 2θ, when analyzed using CuK-α X-ray radiation having wavelength of 1.541 Å.
A composition of the inorganic ion conductor may be confirmed using an X-ray fluorescence spectrometer (XRF).
The inorganic ion conductor may be, for example, at least one selected from In0.5Sb0.5P2O7, SbIII0.5SbV0.5P2O7, Fe0.5Sb0.5P2O7, Al0.5Sb0.5P2O7, Ga0.5Sb0.5P2O7, Y0.5Sb0.5P2O7, Bi0.5Sb0.5P2O7, Fe0.5Nb0.5P2O7, Ga0.5Nb0.5P2O7, Y0.5Nb0.5P2O7, La0.5Nb0.5P2O7, Nd0.5Nb0.5P2O7, Sm0.5Nb0.5P2O7, Fe0.5Ta0.5P2O7, Ga0.5Ta0.5P2O7, Al0.5Ta0.5P2O7, Bi0.5Ta0.5P2O7, In0.5Ta0.5P2O7, Sb0.5Ta0.5P2O7, La0.5Ta0.5P2O7, Sm0.5Ta0.5P2O7, Y0.5Ta0.5P2O7, In0.45Sb0.5P2O7, In0.40Sb0.5P2O7, In0.35Sb0.5P2O7, In0.3Sb0.5P2O7, In0.5Sb0.45P2O7, In0.5Sb0.4P2O7, In0.5Sb0.35P2O7, In0.5Sb0.3P2O7, Fe0.45Sb0.5P2O7, Fe0.40Sb0.5P2O7, Fe0.35Sb0.5P2O7, Fe0.30Sb0.5P2O7, Fe0.5Sb0.45P2O7, Fe0.5Sb0.40P2O7, Fe0.5Sb0.35P2O7, Fe0.5Sb0.3P2O7, Fe0.45Ta0.5P2O7, Fe0.40Ta0.5P2O7, Fe0.35Ta0.5P2O7, Fe0.30Ta0.5P2O7, Fe0.5Ta0.45P2O7, Fe0.5Ta0.4P2O7, Fe0.5Ta0.35P2O7, and Fe0.5Ta0.3P2O7.
Hereinafter, a method of forming an inorganic ion conductor including a trivalent metallic element, a pentavalent metallic element, P, and O is further disclosed.
First, a trivalent metallic element precursor, a pentavalent metallic element precursor, and a phosphorus precursor are contacted to prepare a mixture. The trivalent metallic element precursor may be suitable to provide element A in Formula 1, and the pentavalent metallic element precursor may be suitable to provide element B in Formula 1.
While preparing the mixture, a solvent may be added thereto and mixed therein. If a solvent is used in this regard, all components in the mixture may be uniformly mixed.
The solvent may comprise at least one selected from, distilled water, an alcohol, and a polyol. The alcohol may comprise at least one selected from methanol, ethanol, propanol, isopropyl alcohol, and butanol. The polyol may comprise at least one selected from polyethylene glycol, polypropylene glycol, 1,4-butanediol, pentaerythritol, 2,3-butanediol, ethylene glycol, propylene glycol, trimethylene glycol, 1,4-dihydroxy-2-butene, 1,12-dihydroxyoctadecane, 1,4-dihydroxycyclohexane, 2,2-dimethyl-1,3-propanediol, 2-ethyl-2-butylpropanediol, glycerol, erythritol, sorbitol, mannitol, inositol, trimethylol propane, dipentaerythritol, polybutadiene diol, polytetramethylenediol, and polycaprolactone diol. A content of the solvent may be in a range of about 300 parts to about 800 parts by weight, based on 100 parts by weight of the trivalent metallic element precursor.
When the content of the solvent is within the foregoing range, a viscosity of the composition may be appropriate for handling a preparation of the inorganic ion conductor.
The mixture is stirred. The stirring process may be performed at a temperature of, for example, about 200° C. to about 300° C., specifically about 225° C. to about 275° C.
When the mixture is stirred within the temperature range above, the components of the mixture are uniformly mixed, and water is removed from the composition, and thus the viscosity of the mixture is maintained appropriately. When the viscosity of the mixture is selected as described above, a subsequent thermal treatment process may be efficiently performed, without the composition undergoing phase separation.
Subsequently, the composition is thermally treated at a temperature of about 300° C. to about 1200° C., specifically about 350° C. to about 1100° C., for example, at about 450° C. The thermally treated composition may be ground into a powder having a selected particle size, thereby completing the forming of the inorganic ion conductor.
When the mixture is thermally treated at a temperature within the range above, an inorganic ion conductor having excellent ionic conductivity may be obtained without a structural change. A thermal treatment time may be selected depending on the thermal treatment temperature. For example, the thermal treatment time may be from about 30 minutes to about 20 hours, specifically about 1 hour to about 5 hours, more specifically about 2 hours to about 4 hours.
The thermal treatment may be performed in an inert gas atmosphere or in an air atmosphere.
The trivalent metallic element precursor may comprise at least one selected from an oxide, a chloride, a hydroxide, and a nitrate. The trivalent metallic element precursor may comprise element A of Formula 1, and may be suitable to provide element A of the compound of Formula 1. The trivalent metallic element precursor may comprise at least one selected from indium oxide, antimony oxide, iron oxide, aluminum oxide, gallium oxide, yttrium oxide, bismuth oxide, neodymium oxide, samarium oxide, indium chloride, antimony chloride, iron chloride, aluminum chloride, gallium chloride, yttrium chloride, bismuth chloride, neodymium chloride, samarium chloride, indium hydroxide, antimony hydroxide, iron hydroxide, aluminum hydroxide, gallium hydroxide, yttrium hydroxide, bismuth hydroxide, neodymium hydroxide, samarium hydroxide, indium nitrate, antimony nitrate, iron nitrate, aluminum nitrate, gallium nitrate, yttrium nitrate, bismuth nitrate, neodymium nitrate, and samarium nitrate, for example.
The pentavalent metallic element precursor may comprise at least one selected from an oxide, a chloride, a hydroxide, and a nitrate. The pentavalent metallic element precursor may comprise element B of Formula 1, and may be suitable to provide element B of the compound of Formula 1. The pentavalent metallic element precursor may comprise at least one selected from antimony oxide, niobium oxide, tantalum oxide, antimony hydroxide, niobium hydroxide, tantalum hydroxide, antimony chloride, niobium chloride, tantalum chloride, antimony nitrate, niobium nitrate, tantalum nitrate, vanadium nitrate, vanadium chloride, bismuth nitrate, and bismuth chloride, for example.
A content of the pentavalent metallic element precursor and the trivalent metallic element precursor are appropriately selected to provide the inorganic ion conductor.
The phosphorus precursor may comprise at least one selected from phosphoric acid and phosphonic acid, and the like.
The phosphoric acid may comprise an aqueous phosphoric acid solution, specifically an about 80 to about 100 weight percent (wt %) aqueous phosphoric acid solution. If an 85 wt % aqueous phosphoric acid solution is used, a content of the phosphoric acid may be about 200 parts to about 300 parts by weight, specifically about 225 parts to about 275 parts by weight, based on 100 parts by weight of the trivalent metallic element precursor. When the content of the phosphoric acid is within this range, the phosphoric acid may facilitate preparation of the inorganic ion conductor, taking into consideration a loss of phosphoric acid during the thermal treatment process of the composition for forming the inorganic ion conductor.
In the grinding process, although an average particle diameter obtained is not particularly limited, the product from the thermal treatment may be ground so as to have an average particle diameter of about 50 nanometers (nm) to about 5000 nm, specifically about 100 nm to about 4500 nm.
The inorganic ion conductor powder may be obtained in a form of a molded product by processing and press-molding the powder. The molded product may be used as, for example, an electrolyte.
In the process of press-molding, a cold isostatic press (CIP) process may be used.
In an embodiment, an inorganic ion conductor represented by Formula 1 may be manufactured according to the method of forming an inorganic ion conductor including a trivalent metallic element, a pentavalent metallic element, P, and O described above, except that phosphoric acid is used as a phosphorus precursor.
The inorganic ion conductor has high ionic conductivity, and has an ionic conductivity suitable for a moderate-temperature (e.g., about 100° C. to about 400° C.) non-humidifying fuel cell system.
According to another embodiment, an electrode for a fuel cell including the inorganic ion conductor is provided.
The electrode for a fuel cell includes a catalyst layer including a catalyst and a binder.
The catalyst may comprise at least one selected from platinum (Pt), and an alloy of Pt and at least one metal selected from gold, palladium, rhodium, iridium, ruthenium, tin, molybdenum, cobalt, and chrome. Alternatively, the catalyst may be a supported catalyst in which a catalyst metal is supported on a carbon-based support. For example, the catalyst may comprise at least one catalyst metal selected from Pt, platinum-cobalt (Pt—Co), and platinum-ruthenium (Pt—Ru). To provide a supported catalyst, the catalyst metal may be disposed on a carbon-based support.
The binder may comprise at least one selected from poly(vinylidenefluoride), polytetrafluoroethylene, fluorinated ethylene propylene, styrene butadiene rubber, polyurethane, and tetrafluoroethylene-hexafluoroethylene copolymer. A content of the binder may be about 0.001 part to about 0.5 part by weight, based on 1 part by weight of the catalyst. When the content of the binder is within the range, binding capacity of the catalyst layer to a support is excellent.
According to another embodiment, an electrolyte membrane for a fuel cell including the inorganic ion conductor is provided.
A high performance, high efficiency fuel cell system may be implemented by using the electrolyte membrane and/or the electrode. Also, the inorganic ion conductor may be used as a solid electrolyte in a low-temperature SOFC (e.g., an SOFC operating at about 300° C. to about 500° C.). Also, the inorganic ion conductor may be used in an electrochemical device, such as a catalyst support for purifying an exhaust gas, as an automotive material, or the like.
According to another embodiment, a fuel cell including the inorganic ion conductor is provided.
The fuel cell uses the molded product including the inorganic ion conductor as an electrolyte membrane, which is interposed between a cathode and an anode. The fuel cell has excellent cell potential and output density characteristics at a moderate temperature, e.g., about 100° C. to about 400° C., specifically about 200° C. to about 400° C., in non-humidified conditions.
The electrolyte membrane may be used in an SOFC, a PEMFC, or the like, but is not particularly limited thereto.
Referring to
Although only two unit cells 11 are shown in
As shown in
The electrolyte membrane 100 comprises the inorganic ion conductor disclosed herein.
The catalyst layers 110 and 110′ respectively operate as a fuel electrode and an oxygen electrode, each including a catalyst and a binder therein. The catalyst layers 110 and 110′ may further include a material that may increase an electrochemical surface area of the catalyst.
The first gas diffusion layers 121 and 121′ and the second gas diffusion layers 120 and 120′ may each comprise a porous conductive material such as, for example, carbon sheet or carbon paper. The first gas diffusion layers 121 and 121′ and the second gas diffusion layers 120 and 120′ diffuse oxygen and fuel, respectively, which are supplied by a flow-field of the bipolar plates 20 into entire surfaces of the catalyst layers 110 and 110′.
The fuel cell 1 including the MEA 10 may suitably operate at a temperature of, for example, about 150° C. to about 400° C. A fuel, such as hydrogen, is supplied through the flow-field of one of the bipolar plates 20 into a first catalyst layer, and an oxidant, such as oxygen in air, is supplied through the flow-field of the other bipolar plate 20 to a second catalyst layer. In an embodiment, hydrogen is oxidized into protons in the first catalyst layer, and the protons are conducted to the second catalyst layer through the electrolyte membrane 100. Then, the protons electrochemically react with oxygen in the second catalyst layer to produce water and electrical energy. Hydrogen produced by reforming a hydrocarbon or an alcohol may be used as the fuel. Oxygen may be used as the oxidant and may be supplied in a form of air.
Hereinafter, an exemplary embodiment will be described in further detail with reference to the following examples. These examples shall not limit the scope of the disclosed embodiment.
An inorganic ion conductor of Formula 1 wherein A is In and Q is Sb was manufactured according to the following processes.
In2O3, Sb2O5, and 85 wt % aqueous H3PO4 were mixed in amounts to provide a molar ratio of Sb:In:P=0.5:0.5:2.0-2.8, and distilled water, was added to obtain a mixture. Then, the mixture was stirred at about 300° C. to obtain a viscous paste.
The viscous paste was placed in a ceramic crucible and thermally treated at a temperature of 450° C. for 2.5 hours.
Next, the lump product resulting from the thermal treatment process was ground with a mortar, to prepare In0.5Sb0.5P2O7 as a powder. In consideration of a partial loss of phosphoric acid during the thermal treatment process, an initial content of phosphoric acid added to the inorganic proton conductor was determined to have a final stoichiometric composition of the inorganic ion conductor shown in Example 1 of Table 1 below.
Inorganic ion conductors shown in Table 1 were each obtained as a powder in the same manner as in Example 1, except that a precursor having a molar ratio of A:Q:P corresponding to the molar ratios shown in Table 1 was used to obtain each of inorganic ion conductors of Formula 1 having compositions as shown in Table 1 below.
Inorganic ion conductors were manufactured in the same manner as in Example 1, except that contents of In2O3 and Sb2O5 were each selected to have In and Sb compositions as shown in Table 2 below.
Inorganic ion conductors were manufactured in the same manner as in Example 8, except that contents of Fe2O3 and Nb2O5 were each selected to provide Fe and Nb compositions as shown in Table 3 below.
Inorganic ion conductors were manufactured in the same manner as in Example 8, except that contents of Fe2O3 and Ta2O5 were each selected to provide Fe and Ta compositions as shown in Table 4 below.
SnO2, H3PO4, and distilled water were mixed, and then the mixture was stirred at 300° C. to obtain a viscous paste.
The paste was placed in a ceramic crucible and thermally treated at a temperature of 650° C. for 2.5 hours.
Next, the thermally treated product was ground with a mortar, to prepare an SnP2O7 powder.
SnO2, In2O3, and 85 wt % aqueous H3PO4 were mixed in a molar ratio of Sn:In:P=0.9:0.1:2.0-2.8. Deionized water was added to the mixture and then the mixture was stirred at about 250° C. to obtain a mixed paste having a high viscosity. The mixed paste was thermally treated in an alumina crucible at 650° C. for 2.5 hours.
The lump product resulting from the thermal treatment was ground with a mortar, to prepare Sn0.9In0.1P2O7 as a milk-white powder.
The inorganic ion conductor powders of the Examples and Comparative Examples were each made into a pellet (diameter: about 12 millimeter (mm), thickness: about 2 mm) using a press and a cold isostatic press process (CIP).
A cell was manufactured using gold (Au) electrodes attached on opposite sides of the pellet, and impedance thereof was measured in a non-humidified air atmosphere and evaluated to measure conductivity of the pellet.
The measurement of the impedance was performed at a frequency within a range of about 10 to about 106 Hertz (Hz) and using an alternating current (AC) having an amplitude of 10 milliVolts (mV).
The results of the conductivity analysis are as shown in
Referring to
The inorganic ion conductor powders of Examples 1, 14, 23 to 26, 31 to 33, and 38 to 42 were each made into a pellet (diameter: 12 mm, thickness: about 2 mm) by using a press and CIP.
A cell was manufactured using gold (Au) electrodes on both sides of the pellet, and impedance thereof was measured in a non-humidified air atmosphere and evaluated to measure conductivity of the pellet.
The measurement of the impedance was performed at a frequency within a range of about 10 to about 106 Hz and using an AC having an amplitude of 10 mV.
The results of the conductivity analysis are shown in
Referring to
An XRD analysis (using MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 1, 8, and 14 was performed, and the results thereof are shown in
Referring to
As described above, the inorganic ion conductors of Examples 1, 8, and 14 having a crystal structure very similar to that of a crystalline phase of SnP2O7 and had excellent conductivity, as shown in
An XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 1 and 23 to 26 was performed, and the results thereof is as shown in
Referring to
Also, an XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 1 and 27 to 30 was performed, and the results thereof are as shown in
Referring to
An XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 8 and 31 to 33 was performed, and the results thereof are shown in
Referring to
Also, an XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 8 and 35 to 37 was performed, and the results thereof are shown in
Referring to
An XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 14 and 39 to 42 was performed, and the results thereof is as shown in
Referring to
Also, an XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 14 and 43 to 46 was performed, and the results thereof are shown in
Referring to
An XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 3, 6, and 7 was performed. As a result of the XRD analysis, each crystalline phase of the inorganic ion conductors was analyzed and the results are shown in Table 6 below.
An XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 9 to 13 was performed. As a result of the XRD analysis, each crystalline phase of the inorganic ion conductors was analyzed and the results are shown in Table 7 below.
An XRD analysis (MP-XRD, Xpert PRO, Philips/Power 3 kW, CuK-α X-rays having a wavelength of 1.541 Å) of each of the inorganic ion conductors of Examples 16 to 22 was performed. As a result of the XRD analysis, each crystalline phase of the inorganic ion conductors was analyzed and the results are shown in Table 8 below.
The powders of Example 40 and Comparative Example 2 were press-molded under a pressure of 1×103 kilograms per square centimeter (kg/cm2) using a press and CIP to obtain a pellet (diameter: about 12 mm, thickness: about 1.0 mm) as a press-molded product.
The pellet was used as an electrolyte membrane, and Pt/C-coated carbon papers (electrodes available from ElectroChem, 2 milligrams platinum per square centimeter (mgPt/cm2) were attached to opposite sides of the electrolyte membrane to manufacture a cell.
The cell was placed between two Pt-mesh current collectors to form a Pt-mesh/cell/Pt-mesh stack.
While the stack was placed between upper and lower alumina tubes, the structure was gas-sealed by coating and drying an inorganic sealant on the structure.
In order to test the performance of the fuel cell, non-humidified H2 and non-humidified air were supplied to an anode and a cathode, respectively, at about 50 cubic centimeters per minute (ccm) and about 100 ccm, respectively. Also, while operating the cell at 100° C., 150° C., 200° C., or 250° C., a cell potential and an output density according to a current density were evaluated.
The results of the cell potential evaluation of the cells including the inorganic ion conductor of Example 40 and Comparative Example 2 are shown in
Referring to
The powder of Example 40 was press-molded under a pressure of 1×103 kg/cm2 using a press and CIP to obtain a pellet (diameter: about 12 mm, thickness: about 1.0 mm), thereby preparing an electrolyte. Here, 4 samples of the pellet were prepared with a diameter of about 12 mm and thicknesses of about 0.4 mm, 0.5 mm, 0.75 mm, and 1.0 mm, respectively.
Each pellet was used as an electrolyte membrane, and Pt/C-coated carbon papers (electrodes available from ElectroChem, 2 mgPt/cm2) were attached to opposite sides of each electrolyte membrane to manufacture a cell.
The cell was placed between two Pt-mesh current collectors to form a Pt-mesh/cell/Pt-mesh stack.
While the stack was placed between upper and lower alumina tubes, the structure was gas-sealed by coating and drying an inorganic sealant on the structure.
In order to test the performance of the fuel cell, non-humidified H2 and non-humidified air were supplied to an anode and a cathode, respectively, at about 50 ccm and about 100 ccm, respectively. Also, a cell potential and an output density of the cell according to a current density were evaluated at 225° C.
The results of the evaluation are shown in
Referring to
A TPD test is a method of analyzing components of a desorbed gas while increasing a temperature of a sample at a constant speed.
The inorganic ion conductors of Examples 8 and 33 were dried, and a weight change and a peak intensity of the inorganic ion conductors were observed while increasing a temperature at a rate of 5° C./min. The results are as shown in
Referring to
Referring to
An evaluation of an H2 concentration cell was performed by supplying a gas with a different H2 concentration to both electrode chambers using Pt/C electrodes attached on opposite sides of the pellet, which was prepared using each of the inorganic ion conductors of Examples 24, 32, and 33. An electromotive force was measured at each temperature range of the cell.
The H2 concentration cell was manufactured according to the following processes.
The powder of the inorganic ion conductors of Examples 24, 32, and 33 were further ground with a mortar and then press-molded under a pressure of about 1×103 kg/cm2 to obtain an press-molded product as a pellet having a diameter of about 12 mm.
The thickness of the pellet was about 0.5 mm.
The pellet was used as an electrolyte membrane, and Pt/C-coated carbon papers were attached to opposite sides of the electrolyte membrane to manufacture a cell.
The cell was placed between two Pt-mesh current collectors to form a Pt-mesh/cell/Pt-mesh stack.
While the stack was placed between upper and lower alumina tubes, the structure was gas-sealed by coating and drying an inorganic sealant on the structure.
In order to test the performance of the cell, a gas with a different concentration of H2 was supplied to an anode and a cathode of a battery of Electrochemical Cell 1.
100 vol % H2, Pt/C//electrolyte//Pt/C, 10 vol % H2+Ar Electrochemical Cell 1
The result of the cell evaluation is as shown in
Referring to
The inorganic ion conductors of Examples 8 and 33 were evaluated by using a 1H-mass NMR, and the results thereof are as shown in
Proton mobility may be measured by measuring a peak width at half height of a primary peak through a 1H-NMR analysis. That is, if the peak width at half height is small, the proton mobility is large, and thus the conductivity is excellent.
As described above, according to an embodiment, an inorganic ion conductor with improved conductivity at a moderate temperature range is provided. A fuel cell with improved efficiency may be manufactured using the inorganic ion conductor.
It should be understood that the exemplary embodiment described herein shall be considered in a descriptive sense only and not for purposes of limitation. Descriptions of features, advantages or aspects within each embodiment shall be considered as available for other similar features, advantages, or aspects in other embodiments.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2012-0024452 | Mar 2012 | KR | national |
