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CN105655605B - Solid oxide fuel cell cathod catalyst, composite cathode material and preparation method thereof - Google Patents

Solid oxide fuel cell cathod catalyst, composite cathode material and preparation method thereof Download PDF

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CN105655605B
CN105655605B CN201610027063.5A CN201610027063A CN105655605B CN 105655605 B CN105655605 B CN 105655605B CN 201610027063 A CN201610027063 A CN 201610027063A CN 105655605 B CN105655605 B CN 105655605B
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cathode material
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cathod catalyst
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沈雪松
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9016Oxides, hydroxides or oxygenated metallic salts
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/8647Inert electrodes with catalytic activity, e.g. for fuel cells consisting of more than one material, e.g. consisting of composites
    • H01M4/8652Inert electrodes with catalytic activity, e.g. for fuel cells consisting of more than one material, e.g. consisting of composites as mixture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/88Processes of manufacture
    • H01M4/8825Methods for deposition of the catalytic active composition
    • 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

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Abstract

The invention discloses a kind of solid oxide fuel cell cathod catalysts, composite cathode material and preparation method thereof.The cathod catalyst is the strontium titanates of the perovskite structure of doping, meets following chemical general formulas: (Sr1‑xCx)1‑nTi1‑yDyO3, wherein C is Mg, Ca, one of Ba or a variety of, D Sc, V, Cr, Co, Mn, Ni, Fe, Cu, one of Zn or a variety of;X, y is the molar content of respective element, and 0≤x≤0.95,0 y≤0.95 <;0≤n≤0.08.Preparation method includes ball milling mixing step, sintering step, again ball milling step.The invention also discloses the composite cathode materials of the solid oxide fuel cell comprising above-mentioned cathod catalyst.The performance of solid oxide fuel cell after cathod catalyst of the present invention is added is substantially better than the performance for being not added with the solid oxide fuel cell of cathod catalyst.

Description

Solid oxide fuel cell cathod catalyst, composite cathode material and its preparation Method
Technical field
The present invention relates to a kind of high-performance solid oxidate combined electrode of fuel cell material more particularly to a kind of solid oxygen Compound cathode catalyst for fuel cell, composite cathode material and preparation method thereof.
Background technique
Solid oxide fuel cell is that one kind can be converted the chemical energy in fuel by way of electrochemical reaction For all solid state energy conversion device of electric energy.It is mainly by anode, cathode and electrolyte composition.In general, the sky being passed through in cathode Oxygen reduction reaction occurs at the three phase boundary of cathode internal for gas (oxygen), and the oxonium ion for reacting generation is passed by solid electrolyte The three phase boundary for leading anode interior is in hydrogen and hydroxide reaction occurs, and the electronics for reacting generation passes through external current loop stream Enter cathode and forms closed circuit power generation acting.
The cathode material of solid oxide fuel cell mainly by electronic conductive material and oxygen-ion conductive material mixing and At the oxygen-ion conductive material in cathode is usually made of electrolyte, and three categories electrolyte is after stablizing at present Zirconium oxide (Stabilized-ZrO2), the cerium oxide (Doped-CeO of doping2) and Ishihara invention lanthanum gallate series (US 6844098B1)。
Electronic conductive material in cathode is usually made of five major class: the lanthanum manganate perovskite structural material (JB of doping Goodenough,Theory of the Role of Covalence in the Perovskite-Type Manganites [LaM(II)]MnO3, Physical Review, 1955,100 (2): 564), the cobalt acid lanthanum perovskite structural material (AN of doping Petrov,OF Kononchuk,etc.,Crystal structure,electrical and magnetic properties of La1-xSrxCoO3, Solid State Ionics, 199580 (95): 189), the cadmium ferrite perovskite structural material (Y of doping Teraoka,etc.,Oxygen permeation Through Perovskite-Type Oxides,Chemistry Letters,1985,14(11):1743;Structure and Electrical Properties of La1-xSrxCo1- yFeyO3.Part 1.The system La0.8Sr0.2Co1-yFeyO3,1995,76(3):259;Structure and Electrical Properties of La1-xSrxCo1-yFeyO3.Part 2.The system La1- xSrxCo0.2Fe0.8O31995,76 (3): 273), nickel acid lanthanum perovskite structural material (the R Chiba, etc., An of doping investigation of La Ni1-xFexO3 as a cathode material for solid oxide fuel Cells, Solid State Ionics, 1999,124 (26): 281) and doping K2NiF4Type structure nickelate (SJ Skinner,etc.,Oxygen diffusion and surface exchange in La2-xSrxNiO4 Solid State Ionics,2000,135(1):709;A.Aguadero,etc.,Evalution of the La2Ni1-xCuxO4 system as SOFC cathode materials with 8YSZ and LSGM as electrolyte,Solid State Ionics, 2008,179(11):393)。
Compared to current applicable combination electrode material, higher cathode performance means higher generating efficiency, from And the cost of battery pile can be reduced, it is universal to the commercialization of solid oxide fuel cell play the role of it is vital.
Summary of the invention
In view of the drawbacks of the prior art, one of the objects of the present invention is to provide a kind of solid oxide fuel cell yin Electrode catalyst, the cathode catalyst material can be added in the cathode of other all solids oxide fuel cells, reach raising The purpose of chemical property.
The second object of the present invention is to provide a kind of preparation method of above-mentioned cathod catalyst.
The third object of the present invention is to provide a kind of solid oxide fuel cell use comprising above-mentioned cathod catalyst Composite cathode material.
The fourth object of the present invention is to provide the preparation method of above-mentioned composite cathode material, and this method is simple and easy.
To achieve the goals above, the invention adopts the following technical scheme:
A kind of solid oxide fuel cell cathod catalyst, the cathod catalyst are the perovskite structures of doping Strontium titanates meets following chemical general formulas: (Sr1-xCx)1-nTi1-yDyO3, wherein C is Mg, Ca, one of Ba or a variety of, and D is One of Sc, V, Cr, Co, Mn, Ni, Fe, Cu, Zn or a variety of;X, y is the molar content of respective element, and 0≤x≤ 0.95,0 y≤0.95 <;0≤n≤0.08.
In above-mentioned cathod catalyst, the granularity of the cathod catalyst is no more than 5 as a preferred implementation manner, μm;It is highly preferred that the granularity of the cathod catalyst is 0.005~5 μm;Further, 0≤x≤0.3,0 y≤0.9 <, n= 0。
The preparation method of above-mentioned cathod catalyst, it is preferred to use prepared by solid-phase synthesis, it is highly preferred that the cathode Catalyst fines specific the preparation method is as follows:
Ball milling mixing step: according to the molar content of various elements in prepared cathod catalyst by corresponding amount Raw material SrCO3、TiO2Wet ball grinding is carried out with the oxide to doped chemical until raw material is sufficiently mixed uniformly;
Sintering step: it will be sintered 5~20 hours at 1100 DEG C~1500 DEG C after the product drying after the wet ball grinding;
Sintered product: being carried out wet ball grinding by ball milling step again again until particle diameter meets the requirements.
The composite cathode material of solid oxide fuel cell comprising above-mentioned cathod catalyst.
In above-mentioned composite cathode material, the composite cathode material further includes cathode as a preferred implementation manner, Material and high oxygen-ion conductive material;It is highly preferred that the quality of the cathod catalyst is cathode material, high oxide ion conduction material The 0.05-40% of material and cathod catalyst quality sum;Further, the quality of the high oxygen-ion conductive material is cathode The 30-70% of material and high oxygen-ion conductive material quality sum.
In above-mentioned composite cathode material, the cathode material is perovskite structure as a preferred implementation manner, The ferrite of the doping of the cobaltatess, perovskite structure of the doping of the manganite, perovskite structure of doping, perovskite structure The nickelate and A of doping2NiO4One of nickelate of structure is a variety of.
In above-mentioned composite cathode material, the high oxygen-ion conductive material is metal as a preferred implementation manner, One of lanthanum gallate of the stable zirconium oxide of oxide, the cerium oxide of doped metallic oxide and strontium magnesium cobalt codope is more Kind.
In above-mentioned composite cathode material, the zirconium oxide of the metal oxide stability as a preferred implementation manner, In, the metal oxide is calcium oxide, magnesia, scandium oxide, yttrium oxide, lanthana, praseodymium oxide, neodymia, promethium oxide, oxygen Change one of samarium, europium oxide, gadolinium oxide, terbium oxide, dysprosia, holimium oxide, erbium oxide, thulium oxide, ytterbium oxide and luteium oxide Or it is a variety of;It is highly preferred that the content of the metal oxide is 1- in the zirconium oxide of the metal oxide stability 20mol%.
In above-mentioned composite cathode material, the cerium oxide of the doped metallic oxide as a preferred implementation manner, In, the metal oxide is calcium oxide, magnesia, scandium oxide, yttrium oxide, lanthana, praseodymium oxide, neodymia, promethium oxide, oxygen Change one of samarium, europium oxide, gadolinium oxide, terbium oxide, dysprosia, holimium oxide, erbium oxide, thulium oxide, ytterbium oxide and luteium oxide Or it is a variety of;It is highly preferred that the cerium oxide of the doped metallic oxide meets following chemical general formula: Ce1-xMxO2, wherein 0.05 ≤ x≤0.3, M be one of calcium, magnesium, scandium, yttrium, lanthanum, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium and lutetium or It is a variety of;
Further, the lanthanum gallate of the strontium magnesium cobalt codope meets following chemical general formula: La0.8Sr0.2Ga0.8Mg0.2- xCoxO3, wherein 0≤x≤0.15.
The preparation method of the composite cathode material of above-mentioned solid oxide fuel cell, includes the following steps:
Cathode material powder and high oxygen-ion conductive material powder are mixed and are ground, it is compound to obtain two systems by step 1 Electrode;Wherein the quality of the hyperoxia ion conductive material powder is the 30%~70% of two system combination electrode gross masses;
Cathod catalyst powder is added into the two systems combination electrode, mixes and grinds, obtain three-system for step 2 The composite cathode material;Wherein the quality of the cathod catalyst powder is composite cathode material gross mass described in three-system 0.05-40%.
Compared with prior art, the invention has the following beneficial effects:
Cathode catalyst material of the invention can be added in the cathode of other all solids oxide fuel cells, thus Improve chemical property.The performance of solid oxide fuel cell after cathod catalyst of the present invention is added, which is substantially better than, to be not added with The performance of the solid oxide fuel cell of cathod catalyst.
Detailed description of the invention
Fig. 1 is the power generation performance figure of the monocell after the composite cathode material assembling prepared using the embodiment of the present invention 1;
Fig. 2 is the power generation performance figure of the monocell after the composite cathode material assembling prepared using the embodiment of the present invention 2;
Fig. 3 is the power generation performance figure of the monocell after the composite cathode material assembling prepared using the embodiment of the present invention 3.
Specific embodiment
It, below will present invention is described in further detail in order to keep feature of the invention, effect etc. clearer.
A kind of solid oxide fuel cell cathod catalyst provided by the invention, the cathod catalyst are doping The strontium titanates of perovskite structure meets following chemical general formulas: (Sr1-xCx)1-nTi1-yDyO3, wherein C is Mg, Ca, one of Ba Or a variety of, D Sc, V, Cr, Co, Mn, Ni, Fe, Cu, one of Zn or a variety of;X and y is the Mole percent of respective element Content, and 0≤x≤0.95,0 y≤0.95 <;0≤n≤0.08.
Specifically, cathod catalyst is a kind of strontium titanates (the Doped SrTiO of the perovskite structure of doping3).Doping point It is two kinds:
The first is only in the strontium titanates SrTiO of B location doping3, meet perovskite structure ABO3Or meets location A and lack Sunken perovskite structure A1-nBO3(0≤n≤0.08).I.e. only when B location adulterates, the strontium titanates tool of the perovskite structure of doping There is following chemical general formula: A1-nTi1-yDyO3(i.e. (Sr1-xCx)1-nTi1-yDyO3Middle x=0), wherein D be Sc, V, Cr, Co, Mn, Ni, One of Fe, Cu, Zn or a variety of;0 y≤0.95 < (such as 0.01,0.05,0.1,0.15,0.2,0.25,0.3,0.35, 0.4,0.45,0.5,0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9).
Second is to adulterate to adulterate in B location again in location A.The strontium titanates of the perovskite structure adulterated at this time has as follows Chemical general formula: (Sr1-xCx)1-nTi1-yDyO3, wherein C be Mg, Ca, one of Ba or a variety of, D Sc, V, Cr, Co, Mn, Ni, One of Fe, Cu, Zn or a variety of, 0 x≤0.95 < (such as x be 0.01,0.05,0.1,0.15,0.2,0.25,0.3, 0.35,0.4,0.45,0.5,0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9), 0 y≤0.95 < (for example y is 0.01、0.05、0.1、0.15、0.2、0.25、0.3、0.35、0.4、0.45、0.5、0.55、0.6、0.65、0.7、0.75、0.8、 0.85 or 0.9);0≤n≤0.08.
In summary two kinds of doping situations, cathod catalyst of the invention have following chemical general formulas: (Sr1-xCx)1- nTi1-yDyO3, wherein C be Mg, Ca, one of Ba or a variety of, D Sc, V, Cr, Co, Mn, Ni, Fe, Cu, one of Zn or It is a variety of, 0≤x≤0.95,0 y≤0.95 <;0≤n≤0.08.
In order to realize good effect, the granularity of cathod catalyst of the present invention be preferably not greater than 5 μm (such as: 1-5 μm、0.5-4μm、0.01-0.1μm、0.05-0.2μm、0.001μm、0.05μm、0.3μm、1.5μm、2μm、2.5μm、3μm、3.5 μm,4μm,4.5μm,5μm).It is highly preferred that the granularity of the cathod catalyst is 0.005~5 μm.
In above-mentioned cathod catalyst, the x is preferred are as follows: 0≤x≤0.3, y are preferred are as follows: 0 y≤0.9 <, n are preferably 0.
Above-mentioned cathod catalyst can be by solid reaction process, solution combustion synthetic method, coprecipitation, hydrothermal synthesis method, colloidal sol The tradition inorganic material synthetic method preparation such as gel synthetic method, polymer complex method.Preferably, above-mentioned cathod catalyst uses solid phase It is prepared by reaction method, the specific process is as follows:
Ball milling mixing step: according to the molar content of various elements in prepared cathod catalyst by corresponding amount Raw material SrCO3、TiO2It is straight that wet ball grinding is carried out with the oxide of element representated by the oxide, that is, C and/or D to doped chemical It is sufficiently mixed uniformly to raw material;
Sintering step: by the product after the wet ball grinding it is dry after in 1100 DEG C~1500 DEG C (such as 1110 DEG C, 1150 DEG C, 1200 DEG C, 1250 DEG C, 1300 DEG C, 1350 DEG C, 1400 DEG C, 1450 DEG C, 1490 DEG C) under be sintered 5~20 hours (such as 6h, 8h,12h,15h,18h,19h);
Sintered product: being carried out wet ball grinding by ball milling step again again until particle diameter meets the requirements, finally Obtain cathod catalyst powder.
In the preparation method of above-mentioned cathod catalyst, as a preferred implementation manner, in the ball milling mixing step The medium of the wet ball grinding is ethyl alcohol, ball material mass ratio be 30/1~50/1 (such as 32:1,38:1,42:1,45:1,48: 1), revolving speed is 200~400rpm (such as 210rpm, 250rpm, 300rpm, 320rpm, 340rpm, 360rpm, 380rpm), ball Time consuming be 15-30h (such as 16h, 18h, 20h, for 24 hours, 26h, 28h, 29h).
In the preparation method of above-mentioned cathod catalyst, as a preferred implementation manner, in the ball milling step again In, the medium of the wet ball grinding is ethyl alcohol, ball material mass ratio be 20/1~40/1 (such as 20:1,25:1,30:1,35:1, 40:1), revolving speed be 500~1000rpm (such as 510rpm, 560rpm, 600rpm, 700rpm, 800rpm, 850rpm, 950rpm), Ball-milling Time is 0.5-10h (such as 0.5h, 1h, 2h, 4h, 6h, 8h, 10h).
The preparation method of cathod catalyst of the present invention is simple, is uniformly mixed raw material by first time ball milling, later in sky Sintering makes raw material that high temperature solid state reaction generation perovskite structure oxide ABO occur in gas3Or A1-nBO3, then ball milling again Product after sintering is ground into fine particle powder cathod catalyst powder i.e. of the invention.
A kind of composite cathode material of the solid oxide fuel cell comprising above-mentioned cathod catalyst, the composite cathode Material further includes cathode material and high oxygen-ion conductive material;Preferably, the quality of the cathod catalyst is cathode material, height Oxygen-ion conductive material and cathod catalyst quality sum 0.15-40% (such as 0.16%, 0.2%, 0.3%, 0.4%, 0.8%, 1%, 2%, 5%, 10%, 15%, 20%, 25%, 30%, 35%, 39%);The high oxygen-ion conductive material Quality be cathode material and high oxygen-ion conductive material quality sum 30-70% (such as 31%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 69%).
In above-mentioned composite cathode material, the cathode material is the manganite (Doped of the doping of perovskite structure Manganite-Based Perovskite), cobaltatess (the Doped Cobaltite-Based of the doping of perovskite structure Perovskite), ferrite (Doped Ferrite-Based Perovskite), the perovskite knot of the doping of perovskite structure The nickelate (Doped Nickelate-Based Perovskite) and A of the doping of structure2NiO4Nickelate (the A of structure2NiO4– Type Nickelate) one of or it is a variety of.These types of typical existing cathode material is illustrated below.
The manganite (Doped Manganite-Based Perovskite) of the doping of perovskite structure:
(1) the manganite perovskite AMnO of location A doping3Meet perovskite structure ABO3Or meet location A defect Perovskite structure A1-nBO3(0≤n≤0.08).Wherein location A is the combination of lanthanide series and alkaline-earth metal, i.e., only in location A When doping, the manganite perovskite of location A doping meets following chemical general formula: (Ln1-xCx)1-nMnO3, wherein Ln be La, Ce, One of Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu or a variety of, C Mg, Ca, Sr, one of Ba or It is a variety of;0 < x≤0.95,0≤n≤0.08.
(2) the manganite perovskite AMn of B location doping1-yDyO3Meet perovskite structure ABO3Or location A defect Perovskite structure A1-nBO3(0≤n≤0.08).Wherein B location is the combination of manganese element and variable valency metal, i.e., only mixes in B location When miscellaneous, the manganite perovskite of B location doping meets following chemical general formula: A1-nMn1-yDyO3, wherein D be Sc, Ti, V, Cr, One of Fe, Co, Ni, Cu, Zn or a variety of;A is La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu One of or it is a variety of;0 < y≤0.95,0≤n≤0.08.
(3) when A and B location adulterate simultaneously, the manganite of the doping of perovskite structure meets following chemical general formula: (Ln1-xCx)1-nMn1-yDyO3, wherein Ln is La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, one in Yb, Lu Kind or a variety of, C Mg, Ca, Sr, one of Ba or a variety of, D Sc, Ti, V, Cr, Fe, Co, Ni, Cu, one of Zn or It is a variety of;0 < x≤0.95,0 < y≤0.95,0≤n≤0.08.
In summary three kinds of doping situations, the manganite of the doping for the perovskite structure that the present invention uses preferably satisfy with Lower chemical general formula: (Ln1-xCx)1-nMn1-yDyO3, wherein Ln be La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, One of Yb, Lu or a variety of, C Mg, Ca, Sr, one of Ba or a variety of, D Sc, Ti, V, Cr, Fe, Co, Ni, Cu, Zn One of or it is a variety of;X, y be respective element molar content, and 0≤x≤0.95 (such as x be 0.01,0.05,0.1, 0.15,0.2,0.25,0.3,0.35,0.4,0.45,0.5,0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9), 0 < Y≤0.95 (such as y be 0.01,0.05,0.1,0.15,0.2,0.25,0.3,0.35,0.4,0.45,0.5,0.55,0.6, 0.65,0.7,0.75,0.8,0.85 or 0.9), 0≤n≤0.08, x and y are not zero simultaneously.
The cobaltatess (Doped Cobaltite-Based Perovskite) of the doping of perovskite structure:
(1) the cobaltatess perovskite ACoO of location A doping3Meet perovskite structure ABO3Or meet the calcium of location A defect Perovskite like structure A1-nBO3(0≤n≤0.08).Wherein location A is the combination of lanthanide series and alkaline-earth metal, i.e., only mixes in location A When miscellaneous, the cobaltatess of the doping of perovskite structure meet following chemical general formula: (Ln1-xCx)1-nCoO3, wherein Ln be La, Ce, Pr, One of Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu or a variety of;C is Mg, Ca, Sr, one of Ba or more Kind;0 x≤0.95 <.
(2) the cobaltatess perovskite ACo of B location doping1-yDyO3Meet perovskite structure ABO3Or meet location A defect Perovskite structure A1-nBO3(0≤n≤0.08).Wherein B location is the combination of cobalt element and variable valency metal, i.e., only in B location When doping, the cobaltatess of the doping of perovskite structure meet following chemical general formula: A1-nCo1-yDyO3, wherein A be La, Ce, Pr, One of Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu or a variety of, D Sc, Ti, V, Cr, Mn, Fe, Ni, Cu, One of Zn or a variety of;0 < y≤0.95,0≤n≤0.08.
(3) when A and B location adulterate simultaneously, the cobaltatess of the doping of perovskite structure meet following chemical general formula: (Ln1-xCx)1-n Co1-yDyO3, wherein Ln is La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, one in Yb, Lu Kind or a variety of, C Mg, Ca, Sr, one of Ba or a variety of, D Sc, Ti, V, Cr, Mn, Fe, Ni, Cu, one of Zn or It is a variety of;0 < x≤0.95,0 < y≤0.95,0≤n≤0.08.
In summary three kinds of doping situations, the cobaltatess of the doping for the perovskite structure that the present invention uses preferably satisfy following Chemical general formula: (Ln1-xCx)1-n Co1-yDyO3, wherein Ln be La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, One of Yb, Lu or a variety of, C Mg, Ca, Sr, one of Ba or a variety of, D Sc, Ti, V, Cr, Mn, Fe, Ni, Cu, Zn One of or it is a variety of;X, y be respective element molar content, and 0≤x≤0.95 (such as x be 0.01,0.05,0.1, 0.15,0.2,0.25,0.3,0.35,0.4,0.45,0.5,0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9), 0 < Y≤0.95 (such as y be 0.01,0.05,0.1,0.15,0.2,0.25,0.3,0.35,0.4,0.45,0.5,0.55,0.6, 0.65,0.7,0.75,0.8,0.85 or 0.9) 0≤n≤0.08, x and y are not zero simultaneously.
The ferrite (Doped Ferrite-Based Perovskite) of the doping of perovskite structure:
(1) the ferrite perovskite AFeO of location A doping3Meet perovskite structure ABO3Or meet the calcium of location A defect Perovskite like structure A1-nBO3(0≤n≤0.08).Wherein location A is the combination of lanthanide series and alkaline-earth metal, i.e., only mixes in location A When miscellaneous, the ferrite of the doping of perovskite structure meets following chemical general formula: (Ln1-xCx)1-nFeO3, wherein Ln be La, Ce, Pr, One of Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu or a variety of;C is Mg, Ca, Sr, one of Ba or more Kind;0 x≤0.95 <.
(2) the ferrite perovskite AFe of B location doping1-yDyO3Meet perovskite structure ABO3Or meet location A defect Perovskite structure A1-nBO3(0≤n≤0.08).Wherein B location is the combination of ferro element and variable valency metal, i.e., only in B location When doping, the ferrite of the doping of perovskite structure meets following chemical general formula: A1-nFe1-yDyO3, wherein A be La, Ce, Pr, One of Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu or a variety of;D is Sc, Ti, V, Cr, Co, Mn, Ni, Cu, One of Zn or a variety of;0 y≤0.95 <;
(3) when A and B location adulterate simultaneously, the ferrite of the doping of perovskite structure meets following chemical general formula: (Ln1-xCx)1-nFe1-yDyO3, wherein Ln is La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, one in Yb, Lu Kind is a variety of;C is Mg, Ca, Sr, one of Ba or a variety of;D is Sc, Ti, V, Cr, Co, Mn, Ni, Cu, one of Zn or It is a variety of;0 x≤0.95 <;0 y≤0.95 <;0≤n≤0.08.
In summary three kinds of doping situations, the ferrite of the doping for the perovskite structure that the present invention uses preferably satisfies following Chemical general formula: (Ln1-xCx)1-n Fe1-yDyO3, wherein Ln be La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, One of Yb, Lu or a variety of, C Mg, Ca, Sr, one of Ba or a variety of, D Sc, Ti, V, Cr, Co, Mn, Ni, Cu, Zn One of or it is a variety of;;X, y be respective element molar content, and 0≤x≤0.95 (such as x be 0.01,0.05, 0.1,0.15,0.2,0.25,0.3,0.35,0.4,0.45,0.5,0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9), 0 y≤0.95 < (such as y be 0.01,0.05,0.1,0.15,0.2,0.25,0.3,0.35,0.4,0.45,0.5, 0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9) 0≤n≤0.08, x and y are not zero simultaneously.
The nickelate (Doped Nickelate-Based Perovskite) of the doping of perovskite structure:
(1) the nickelate perovskite ANiO of location A doping3Meet perovskite structure ABO3Or meet the calcium of location A defect Perovskite like structure A1-nBO3(0≤n≤0.08).Wherein location A is the combination of lanthanide series and alkaline-earth metal, i.e., only mixes in location A When miscellaneous, the nickelate of the doping of perovskite structure meets following chemical general formula: (Ln1-xCx)1-nNiO3, wherein Ln be La, Ce, Pr, One of Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu or a variety of;C is Mg, Ca, Sr, one of Ba or more Kind;0 x≤0.95 <.
(2) the ferrite perovskite ANi of B location doping1-yDyO3Meet perovskite structure ABO3Or meet location A defect Perovskite structure A1-nBO3(0≤n≤0.08).Wherein B location is the combination of nickel element and variable valency metal, i.e., only in B location When doping, the ferrite of the doping of perovskite structure meets following chemical general formula: A1-nNi1-yDyO3, wherein A be La, Ce, Pr, One of Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu or a variety of;D is Sc, Ti, V, Cr, Co, Mn, Fe, Cu, One of Zn or a variety of;0 y≤0.95 <;
(3) when A and B location adulterate simultaneously, the nickelate of the doping of perovskite structure meets following chemical general formula: (Ln1-xCx)1-nNi1-yDyO3, wherein Ln is La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, one in Yb, Lu Kind is a variety of;C is Mg, Ca, Sr, one of Ba or a variety of;D is Sc, Ti, V, Cr, Co, Mn, Fe, Cu, one of Zn or It is a variety of;0 x≤0.95 <;0 y≤0.95 <;0≤n≤0.08.
In summary three kinds of doping situations, the nickelate of the doping for the perovskite structure that the present invention uses preferably satisfies following Chemical general formula: (Ln1-xCx)1-n Ni1-yDyO3, wherein Ln be La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, One of Yb, Lu or a variety of, C Mg, Ca, Sr, one of Ba or a variety of, D Sc, Ti, V, Cr, Co, Mn, Fe, Cu, Zn One of or it is a variety of;;X, y be respective element molar content, and 0≤x≤0.95 (such as x be 0.01,0.05, 0.1,0.15,0.2,0.25,0.3,0.35,0.4,0.45,0.5,0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9), 0 y≤0.95 < (such as y be 0.01,0.05,0.1,0.15,0.2,0.25,0.3,0.35,0.4,0.45,0.5, 0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9), 0≤n≤0.08, x and y are not zero simultaneously.
A2BO4Nickelate (the A of structure2NiO4- type Nickelate):
(1) the nickelate A of location A doping2NiO4Meet structure A2BO4Or meet the structure (A of location A defect2)1-nBO4 (0≤n≤0.08).Wherein location A is the combination of lanthanide series and alkaline-earth metal, i.e., only when location A adulterates, A2BO4Structure Nickelate meets following chemical general formula: (Ln2-xCx)1-nNiO4, wherein Ln be La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, One of Ho, Er, Tm, Yb, Lu or a variety of;C is Mg, Ca, Sr, one of Ba or a variety of;0 x≤1.8 <.
(2) the nickelate A of B location doping2NiO4Meet structure A2BO4Or meet the structure (A of location A defect2)1-nBO4 (0≤n≤0.08).Wherein B location is the combination of nickel element and variable valency metal, i.e., only when B location adulterates, A2BO4The nickel of structure Hydrochlorate meets following chemical general formula: A2Ni1-yDyO4, wherein A be La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, One of Yb, Lu or a variety of, D Sc, Ti, V, Cr, Co, Mn, Fe, Cu, one of Zn or a variety of;0 y≤0.95 <.
(3) when A and B location adulterate simultaneously, A2BO4The nickelate of structure meets following chemical general formula: (Ln2-xCx)1- nNi1-yDyO4, wherein Ln is La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, one of Lu or a variety of;C For Mg, Ca, Sr, one of Ba or a variety of;D is Sc, Ti, V, Cr, Co, Mn, Fe, Cu, one of Zn or a variety of;0 < x≤ 1.8;0 y≤0.95 <;0≤n≤0.08.
In summary three kinds of doping situations, the A that the present invention uses2BO4It is logical that the nickelate of structure preferably satisfies following chemistry Formula: (Ln2-xCx)1-nNi1-yDyO4, wherein Ln is La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, in Yb, Lu It is one or more, C Mg, Ca, Sr, one of Ba or a variety of, D Sc, Ti, V, Cr, Co, Mn, Fe, Cu, one of Zn Or it is a variety of;X, y be respective element molar content, and 0≤x≤1.8 (such as x be 0.01,0.05,0.1,0.15,0.2, 0.25、0.3、0.35、0.4、0.45、0.5、0.55、0.6、0.65、0.7、0.75、0.8、0.85、0.9、1、1.1、1.2、1.3、 1.4,1.5,1.6,1.7), 0 y≤0.95 < (such as y is 0.01,0.05,0.1,0.15,0.2,0.25,0.3,0.35,0.4, 0.45,0.5,0.55,0.6,0.65,0.7,0.75,0.8,0.85 or 0.9), 0≤n≤0.08, x and y are not zero simultaneously.
In above-mentioned composite cathode material, the high oxygen-ion conductive material be preferably metal oxide stability zirconium oxide, One of lanthanum gallate of the cerium oxide of doped metallic oxide and strontium magnesium cobalt codope is a variety of.Below to these three hyperoxia from Subconductivity material is discussed in detail.
Zirconium oxide (the Stabilized ZrO of metal oxide stability2) in, common metal oxide is calcium oxide (CaO), one of magnesia (MgO) and some rare earth oxides or a variety of, the rare earth oxide such as oxygen Change yttrium (Y2O3), scandium oxide (Sc2O3), lanthana (La2O3), praseodymium oxide (Pr2O3), neodymia (Nd2O3), promethium oxide (Pm2O3)、 Samarium oxide (Sm2O3), europium oxide (Eu2O3), gadolinium oxide (Gd2O3), terbium oxide (Tb2O3), dysprosia (Dy2O3), holimium oxide (Ho2O3), erbium oxide (Er2O3), thulium oxide (Tm2O3), ytterbium oxide (Yb2O3), luteium oxide (Lu2O3).Preferably, in the gold Belong in the stable zirconium oxide of oxide, the content of the metal oxide be 1-20mol% (such as 2mol%, 4mol%, 5mol%, 6mol%, 7mol%, 8mol%, 9mol%, 10mol%, 11mol%, 12mol%, 13mol%, 14mol%, 15mol%, 17mol%, 19mol%).Specifically, general material has 8mol%Y2O3The ZrO of doping2[(Y2O3)0.08 (ZrO2)0.92], 10mol%Sc2O3The ZrO of doping2[(Sc2O3)0.1(ZrO2)0.9], 10mol%Sc2O3And 1mol%CeO2Doping ZrO2[(Sc2O3)0.1(CeO2)0.01(ZrO2)0.89], 10mol%Sc2O3And 1mol%Al2O3The ZrO of doping2[(Sc2O3)0.1 (Al2O3)0.01(ZrO2)0.89], 6mol%Sc2O3And 1mol%Al2O3The ZrO of doping2[(Sc2O3)0.06(Al2O3)0.01 (ZrO2)0.93]。
Cerium oxide (the Doped CeO of doped metallic oxide2) in, common metal oxide is calcium oxide (CaO), oxygen Change one of magnesium (MgO) and some rare earth oxides or a variety of.The rare earth oxide can be yttrium oxide (Y2O3), scandium oxide (Sc2O3), lanthana (La2O3), praseodymium oxide (Pr2O3), neodymia (Nd2O3), promethium oxide (Pm2O3), oxidation Samarium (Sm2O3), europium oxide (Eu2O3), gadolinium oxide (Gd2O3), terbium oxide (Tb2O3), dysprosia (Dy2O3), holimium oxide (Ho2O3)、 Erbium oxide (Er2O3), thulium oxide (Tm2O3), ytterbium oxide (Yb2O3), luteium oxide (Lu2O3).These metal oxides MO or M2O3 CeO after doping2Are as follows: Ce1-xMxO2(0.05≤x≤0.3), M be above-mentioned metallic element, that is, calcium, magnesium, yttrium, scandium, lanthanum, praseodymium, neodymium, One of promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium and lutetium are a variety of.
Lanthanum gallate (Sr, Mg, and Co the co-doped LaGaO of strontium magnesium cobalt codope3) in, the strontium magnesium cobalt codope Lanthanum gallate meet following chemical general formula: La0.8Sr0.2Ga0.8Mg0.2-xCoxO3(0≤x≤0.15, for example, x be 0,0.05, 0.1、0.12、0.14)。
Above-mentioned cathode material powder and high oxygen-ion conductive material powder can be by the anti-methods of solid phase, solution combustion synthetic method, altogether The tradition inorganic material synthetic method preparation such as the precipitation method, hydrothermal synthesis method, collosol and gel synthetic method, polymer complex method.It can also be straight It connects from companies such as Fuel Cell Materials and buys.
The preparation method of the composite cathode material of above-mentioned solid oxide fuel cell, includes the following steps:
Cathode material powder and high oxygen-ion conductive material powder are mixed and are ground, it is compound to obtain two systems by step 1 Electrode;Wherein the quality of the hyperoxia ion conductive material powder is the 30%~70% of two system combination electrode gross masses;
Above-mentioned cathod catalyst powder is added into the two systems combination electrode, mixes and grinds, obtain three for step 2 Composite cathode material described in system;Wherein the quality of the cathod catalyst powder is the total matter of composite cathode material described in three-system The 0.05-40% of amount.
In the preparation method of above-mentioned composite cathode material, as a preferred implementation manner, in said step 1, institute State cathode material powder particle partial size be 0.3~1.5 μm (such as: 0.4 μm, 0.5-1 μm, 0.5 μm, 0.6 μm, 0.7 μm, 0.8 μm,0.9μm,1.2μm,1.3μm,1.4μm);The powder particle partial size of the high oxygen-ion conductive material is 0.3~1.5 μm of (ratio Such as: 0.3-0.5 μm, 0.5-1 μm, 0.4 μm, 0.5 μm, 0.6 μm, 0.7 μm, 0.8 μm, 0.9 μm, 1.0 μm, 1.1 μm, 1.4 μm).
In the preparation method of above-mentioned composite cathode material, as a preferred implementation manner, in the step 2, institute State the partial size of cathod catalyst powder no more than 5 μm (such as: 1-5 μm, 0.5-4 μm, 0.01-0.1 μm, 0.05-0.2 μm, 0.001μm,0.05μm,0.3μm,1.5μm,2μm,2.5μm,3μm,3.5μm,4μm,4.5μm,5μm,).It is highly preferred that described The granularity of cathod catalyst is 0.005~5 μm.
In the preparation method of above-mentioned composite cathode material, as a preferred implementation manner, in the step 1 and institute It states in step 2, the grinding is wet ball grinding, specific process parameter are as follows: 200~400rpm of the range of speeds (such as 210rpm, 250rpm, 28rpm, 310rpm, 330rpm, 360rpm, 390rpm), ball material quality is than (the ratio of range 20/1~40/1 Such as 20:1,25:1,30:1,35:1,40:1), medium is ethyl alcohol, Ball-milling Time 20-24h (such as 21h, 22h, 23h).This two Grinding in step is mainly used for for various materials being uniformly mixed.
The application method of above-mentioned three-system composite cathode material, comprising: firstly, by above-mentioned three-system composite cathode material with Organic bond is mixed and made into electrode slurry;Then, the electrode slurry is printed in electrolyte using the method for silk-screen printing Surface, thickness of electrode are controlled at 10~100 μm;According to the difference of type of electrodes, by the electrode in 900 DEG C~1300 DEG C (ratios Such as: 910 DEG C, 950 DEG C, 1000 DEG C, 1100 DEG C, 1200 DEG C, 1250 DEG C, 1290 DEG C) in sintering 1h~10h (such as: 2h, 3h, 5h、6h、7h、8h、9h)。
Below with manganite-metal oxide stability zirconium oxide-cathod catalyst system of the doping of perovskite structure For column composite cathode material, it was demonstrated that add the feature performance benefit of the composite cathode material of catalyst, specifically tested using full battery The generated output of method test solid oxide fuel cell monocell.It is also provided with the normal cell of comparison in embodiments, (the Sc that the electrolyte of the contrast standard battery uses with a thickness of 200 μm2O3)0.10(CeO2)0.01(ZrO2)0.89Electrolyte, electrode Material powder is obtained from Fuel Cell Materials company.In addition, using the method for silk-screen printing in electrolyte sheet side Print the NiO- (Sc of top surface area 0.64cm2O3)0.10(CeO2)0.01(ZrO2)0.89Anode slurry as anode, it is dry after Sintering 1~5 in 1100 DEG C~1400 DEG C (contrast standard battery used in the following embodiment is carried out at 1300 DEG C) Hour (contrast standard battery used in the following embodiment has been sintered 4h).Silk-screen printing is used in the other side of electrolyte sheet Method printing top surface area 0.64cm (La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89Cathode slurry As standard cathode, at 1100 DEG C~1300 DEG C, (contrast standard battery used in the following embodiment is 1200 after drying Carried out at DEG C) 1~5 hour (contrast standard battery used in the following embodiment has been sintered 4h) of middle sintering.
The monocell performance test methods of following embodiment and normal cell are as follows: monocell is carried out under 800 DEG C of furnace temperature Performance test, anode are passed through the hydrogen for being mixed with 3vol% vapor, and cathode is passed through air.
The manganite of the doping of various perovskite structures used in the following embodiment and metal oxide stability Zirconium oxide is purchased from Fuel Cell Materials.
Embodiment 1
(1) strontium titanates of the perovskite structure of Fe2O3 doping is synthesized with solid-phase synthesis, chemical formula is as follows: SrTi1- yFeyO3;Y=0.35.
A. by the SrCO of purity >=99.9%3、TiO2、Fe2O3Three kinds of raw materials are according to chemical formula SrTi0.65Fe0.35O3Middle gold Belong to the mixing of element molar percentage, and ball milling 24 hours in ethanol medium, revolving speed 300rpm, ball material mass ratio 40/1.
B. the product after ball milling is dry, it is sintered 10 hours in 1400 DEG C later.
C. after being sintered, in alcoholic media, revolving speed 800rpm, ball milling 10 hours under conditions of ball material mass ratio 35/1 Grain average grain diameter is 0.06 μm.
(2) in two system composite cathode material of standard
(La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89(wherein (Sc2O3)0.10(CeO2)0.01 (ZrO2)0.89Quality account for entire standard composite cathode material quality 50%, average particle size is 1.2 μm) in above-mentioned cathode be added urge Agent is mixed and is ground, and grinding condition is as follows: ball milling 24 hours in ethanol medium, revolving speed 300rpm, ball material mass ratio 40/1, Finally obtain the composite cathode material powder of three-system.Wherein, above-mentioned cathod catalyst accounts for the composite cathode material powder of three-system The mass percent at end is 10% (i.e. SrTi0.65Fe0.35O3/(La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01 (ZrO2)0.89=1/9.
It is tested using performance of the following methods to the composite cathode material powder of the three-system:
Firstly, organic bond is added into above-mentioned composite cathode powder is made composite cathode slurry, wherein above-mentioned compound The mass ratio of cathode powder and organic binder is 5:5.
Then, (the Sc using the method for silk-screen printing at 200 μm2O3)0.10(CeO2)0.01(ZrO2)0.89Electrolyte sheet one NiO- (the Sc of side printing top surface area 0.64cm2O3)0.10(CeO2)0.01(ZrO2)0.89Anode slurry as anode, it is dry after It is sintered 4 hours in 1300 DEG C.The upper of top surface area 0.64cm is printed using the method for silk-screen printing in the other side of electrolyte sheet Composite cathode slurry is stated as cathode, is sintered 4 hours in 1200 DEG C after dry.
Fig. 1 shows addition 10%SrTi0.65Fe0.35O3(the La of powder0.8Sr0.2)0.98MnO3-(Sc2O3)0.10 (CeO2)0.01(ZrO2)0.89The monocell power generation performance of composite cathode, it can be seen from the figure that two system composite cathode of standard 10%SrTi is added in material0.65Fe0.35O3Battery performance is better than normal cell performance afterwards, the maximum power density of battery from 501mWcm-2Increase to 600mWcm-2
Embodiment 2
In three-system composite cathode material manufactured in the present embodiment, except the cathod catalyst SrTi of addition0.65Fe0.35O3's Content is different from other than embodiment 1, other are same as Example 1, in the present embodiment, cathod catalyst SrTi0.65Fe0.35O3The mass percent for accounting for the composite cathode material powder of three-system is 20% (i.e. SrTi0.65Fe0.35O3/ (La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89=2/8.
To the performance methodology of the composite cathode material powder of three-system manufactured in the present embodiment with embodiment 1.As a result referring to Fig. 2, as shown, 20%SrTi is added into two system composite cathode material of standard0.65Fe0.35O3Battery performance is better than mark afterwards Quasi- battery performance, the maximum power density of battery is from 501mWcm-2Increase to 822mWcm-2
Embodiment 3
In three-system composite cathode material manufactured in the present embodiment, except the cathod catalyst SrTi of addition0.65Fe0.35O3's Content is different from other than embodiment 1, other are same as Example 1, in the present embodiment, cathod catalyst SrTi0.65Fe0.35O3The mass percent for accounting for the composite cathode material powder of three-system is 40% (i.e. SrTi0.65Fe0.35O3/ (La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89=4/6.
To the performance methodology of the composite cathode material powder of three-system manufactured in the present embodiment with embodiment 1.As a result referring to Fig. 3, as shown, 40%SrTi is added into two system composite cathode material of standard0.65Fe0.35O3Battery performance is better than mark afterwards Quasi- battery performance, the maximum power density of battery is from 501mWcm-2Increase to 540mWcm-2
Embodiment 4
In three-system composite cathode material manufactured in the present embodiment, except the cathod catalyst SrTi of addition0.95Fe0.05O3's Chemical composition and content are different from other than embodiment 1, other are same as Example 1, in the present embodiment, cathod catalyst SrTi0.95Fe0.05O3The mass percent for accounting for the composite cathode material powder of three-system is 20% (i.e. SrTi0.95Fe0.05O3/ (La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89=2/8.
To the performance methodology of the composite cathode material powder of three-system manufactured in the present embodiment with embodiment 1.The results show that 20%SrTi is added into two system composite cathode material of standard0.95Fe0.05O3Battery performance is better than normal cell performance, electricity afterwards The maximum power density in pond is 720mWcm-2
Embodiment 5
In three-system composite cathode material manufactured in the present embodiment, except the cathod catalyst SrTi of addition0.1Fe0.9O3Change It learns composition and content is different from other than embodiment 1, other are same as Example 1, in the present embodiment, cathod catalyst SrTi0.1Fe0.9O3The mass percent for accounting for the composite cathode material powder of three-system is 20% (i.e. SrTi0.1Fe0.9O3/ (La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89=2/8.
To the performance methodology of the composite cathode material powder of three-system manufactured in the present embodiment with embodiment 1.The results show that 20%SrTi is added into two system composite cathode material of standard0.1Fe0.9O3Battery performance is better than normal cell performance, battery afterwards Maximum power density be 542mWcm-2
Embodiment 6
In three-system composite cathode material manufactured in the present embodiment, except the cathod catalyst of addition Sr0.8Ba0.2Ti0.65Fe0.35O3Chemical composition and content be different from embodiment 1 other than, other are same as Example 1, this In embodiment, cathod catalyst Sr0.8Ba0.2Ti0.65Fe0.35O3Account for the mass percent of the composite cathode material powder of three-system For 20% (i.e. Sr0.8Ba0.2Ti0.65Fe0.35O3/(La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89=2/ 8。
To the performance methodology of the composite cathode material powder of three-system manufactured in the present embodiment with embodiment 1.The results show that 20%Sr is added into two system composite cathode material of standard0.8Ba0.2Ti0.65Fe0.35O3Battery performance is better than normal cell afterwards Can, the maximum power density of battery is 540mWcm-2
Embodiment 7
In three-system composite cathode material manufactured in the present embodiment, except the cathod catalyst of addition Sr0.8Ca0.2Ti0.65Fe0.35O3Chemical composition and content be different from embodiment 1 other than, other are same as Example 1, this In embodiment, cathod catalyst Sr0.8Ca0.2Ti0.65Fe0.35O3Account for the mass percent of the composite cathode material powder of three-system For 20% (i.e. Sr0.8Ca0.2Ti0.65Fe0.35O3/(La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89=2/ 8。
To the performance methodology of the composite cathode material powder of three-system manufactured in the present embodiment with embodiment 1.The results show that 20%Sr is added into two system composite cathode material of standard0.8Ca0.2Ti0.65Fe0.35O3Battery performance is better than normal cell afterwards Can, the maximum power density of battery is 538mWcm-2
Embodiment 8
In three-system composite cathode material manufactured in the present embodiment, except the cathod catalyst of addition Sr0.8Mg0.2Ti0.65Fe0.35O3Chemical composition and content be different from embodiment 1 other than, other are same as Example 1, this In embodiment, cathod catalyst Sr0.8Mg0.2Ti0.65Fe0.35O3Account for the mass percent of the composite cathode material powder of three-system For 20% (i.e. Sr0.8Mg0.2Ti0.65Fe0.35O3/(La0.8Sr0.2)0.98MnO3-(Sc2O3)0.10(CeO2)0.01(ZrO2)0.89=2/ 8。
To the performance methodology of the composite cathode material powder of three-system manufactured in the present embodiment with embodiment 1.The results show that 20%Sr is added into two system composite cathode material of standard0.8Mg0.2Ti0.65Fe0.35O3Battery performance is better than normal cell afterwards Can, the maximum power density of battery is 571mWcm-2
Comparative example 1
In the three-system composite cathode material of this comparison preparation, except the cathod catalyst SrTi of addition0.65Fe0.35O3Amount Other than embodiment 1, other are same as Example 1, in the present embodiment, cathod catalyst SrTi0.65Fe0.35O3It accounts for The mass percent of the composite cathode material powder of three-system is 0.1% (i.e. SrTi0.65Fe0.35O3/(La0.8Sr0.2)0.98MnO3- (Sc2O3)0.10(CeO2)0.01(ZrO2)0.89=0.01/9.99.
To the performance methodology of the composite cathode material powder of three-system manufactured in the present embodiment with embodiment 1.The results show that 0.1%SrTi is added into two system composite cathode material of standard0.65Fe0.35O3Afterwards battery performance substantially with normal cell performance Maintain an equal level, the maximum power density of battery is 502mWcm-2
Comparative example 2
By cathod catalyst SrTi0.65Fe0.35O3It is added to (Sc2O3)0.10(CeO2)0.01(ZrO2)0.89(average particle size is 1.2 μm) in, wherein cathod catalyst and (Sc2O3)0.10(CeO2)0.01(ZrO2)0.89Mass ratio be 2:8, by the two mix simultaneously Grinding, grinding condition are as follows: ball milling 24 hours in ethanol medium, revolving speed 300rpm, ball material mass ratio 40/1 finally obtain compound Cathode material powder.
It uses and is surveyed with performance of the identical method of embodiment 1 to composite cathode material powder prepared by this comparative example Examination, the maximum power density of battery are 350mWcm-2

Claims (13)

1. a kind of composite cathode material of solid oxide fuel cell, which is characterized in that the composite cathode material includes Cathod catalyst, cathode material and high oxygen-ion conductive material;
The cathod catalyst is the strontium titanates of the perovskite structure of doping, meets following chemical general formulas: (Sr1-xCx)1-nTi1- yDyO3, wherein C is Mg, Ca, one of Ba or a variety of, D Sc, V, Cr, Co, Mn, Ni, Fe, Cu, one of Zn or more Kind;X, y is the molar content of respective element, and 0≤x≤0.95,0 y≤0.95 <;0≤n≤0.08;
The granularity of the cathod catalyst is no more than 5 μm;
The quality of the cathod catalyst is cathode material, high oxygen-ion conductive material and cathod catalyst quality sum 0.2-40%;
The cathode material is cobaltatess, the perovskite of the doping of the manganite, perovskite structure of the doping of perovskite structure The nickelate and A of the doping of the ferrite, perovskite structure of the doping of structure2NiO4One of nickelate of structure is a variety of.
2. composite cathode material according to claim 1, which is characterized in that the quality of the high oxygen-ion conductive material is yin The 30-70% of pole material and high oxygen-ion conductive material quality sum.
3. composite cathode material according to claim 1 or claim 2, which is characterized in that the granularity of the cathod catalyst is 0.005 ~5 μm.
4. composite cathode material according to claim 1 or claim 2, which is characterized in that the chemical general formula of the cathod catalyst (Sr1-xCx)1-nTi1-yDyO3In, 0≤x≤0.3,0 y≤0.9 <, n=0.
5. composite cathode material according to claim 1 or claim 2, which is characterized in that the cathod catalyst powder uses solid phase It is prepared by synthetic method.
6. composite cathode material according to claim 5, which is characterized in that the specific preparation side of the cathod catalyst powder Method is as follows:
Ball milling mixing step: according to the molar content of various elements in prepared cathod catalyst by the raw material of corresponding amount SrCO3、TiO2Wet ball grinding is carried out with the oxide to doped chemical until raw material is sufficiently mixed uniformly;
Sintering step: it will be sintered 5~20 hours at 1100 DEG C~1500 DEG C after the product drying after the wet ball grinding;
Sintered product: being carried out wet ball grinding by ball milling step again again until particle diameter meets the requirements.
7. composite cathode material according to claim 1 or 2, which is characterized in that the high oxygen-ion conductive material is gold Belong to one of lanthanum gallate of the stable zirconium oxide of oxide, the cerium oxide of doped metallic oxide and strontium magnesium cobalt codope or more Kind.
8. composite cathode material according to claim 7, which is characterized in that the zirconium oxide of the metal oxide stability In, the metal oxide is calcium oxide, magnesia, scandium oxide, yttrium oxide, lanthana, praseodymium oxide, neodymia, promethium oxide, oxygen Change one of samarium, europium oxide, gadolinium oxide, terbium oxide, dysprosia, holimium oxide, erbium oxide, thulium oxide, ytterbium oxide and luteium oxide Or it is a variety of.
9. composite cathode material according to claim 8, which is characterized in that in the zirconium oxide of the metal oxide stability In, the content of the metal oxide is 1-20mol%.
10. composite cathode material according to claim 7, which is characterized in that the cerium oxide of the doped metallic oxide In, the metal oxide is calcium oxide, magnesia, scandium oxide, yttrium oxide, lanthana, praseodymium oxide, neodymia, promethium oxide, oxygen Change one of samarium, europium oxide, gadolinium oxide, terbium oxide, dysprosia, holimium oxide, erbium oxide, thulium oxide, ytterbium oxide and luteium oxide Or it is a variety of.
11. composite cathode material according to claim 10, which is characterized in that the cerium oxide of the doped metallic oxide Meet following chemical general formula: Ce1-xMxO2, wherein 0.05≤x≤0.3, M be calcium, magnesium, scandium, yttrium, lanthanum, praseodymium, neodymium, promethium, samarium, europium, One of gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium and lutetium are a variety of.
12. composite cathode material according to claim 7, which is characterized in that the lanthanum gallate of the strontium magnesium cobalt codope is full The following chemical general formula of foot: La0.8Sr0.2Ga0.8Mg0.2-xCoxO3, wherein 0≤x≤0.15.
13. a kind of method for the composite cathode material for preparing any solid oxide fuel cell of claim 1-12, It is characterized by comprising the following steps:
Cathode material powder and high oxygen-ion conductive material powder are mixed and are ground, obtain two system combination electrodes by step 1; Wherein the quality of the hyperoxia ion conductive material powder is the 30%~70% of two system combination electrode gross masses;
Cathod catalyst powder is added into the two systems combination electrode, mixes and grinds, obtain described in three-system for step 2 Composite cathode material;Wherein the quality of the cathod catalyst powder is the 0.2- of composite cathode material gross mass described in three-system 40%.
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