CN1962456A - Process for preparing solid oxide fuel cell cathode material nanometer powder - Google Patents
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- CN1962456A CN1962456A CNA2006100705648A CN200610070564A CN1962456A CN 1962456 A CN1962456 A CN 1962456A CN A2006100705648 A CNA2006100705648 A CN A2006100705648A CN 200610070564 A CN200610070564 A CN 200610070564A CN 1962456 A CN1962456 A CN 1962456A
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Abstract
The invention discloses a preparing method of cathode nanometer powder of solid oxide fuel battery in the inorganic material preparing domain, which comprises the following steps: adopting nitrate of La, Co, Sr and Fe as raw material; allocating even solution; adding organic monomer acrylamide and cross-linking agent N, N'-methylene diacrylamide into composite solution; stirring evenly; adding initiator ammonium peroxodisulfate solution; placing the solution in the baker at 60-80 Deg C for 20-60min; solidifying the composite solution into gel; making gel into loose, flocculent and porous former through dehydrating and predisposing; sintering former; obtaining the grain size of perovskite structure nanometer powder at 20-150nm without other impurities; changing the adding quantity of acrylamide and cross-linking agent to prepare different grain size nanometer powder of perovskite structure.
Description
Technical field
The present invention relates to preparation method, belong to field of inorganic material preparing technology as Solid Oxide Fuel Cell (SOFC) cathode material perovskite structure nano-powder.
Technical background
At present, in the interior primary energy source consumption structure of world wide, still based on fossil class energy expenditure, but the fossil class energy is the unholiness energy, when satisfying the energy demand of people's overwhelming majority, also discharged a large amount of waste water,waste gas and industrial residue, caused acid rain harm, Greenhouse effect, depletion of the ozone layer and potential the feminize harm and the global environmental problems such as threat of Chemical Time Bomb to nature.Fuel cell is that the chemical energy of fuel directly is transformed into the efficient energy conversion device of electric energy without carnot's working cycle, greatly reduces the degree of these pollutions.In alkaline fuel cell, phosphoric acid salt fuel cell, molten carbonate fuel cell, Proton Exchange Membrane Fuel Cells and Solid Oxide Fuel Cell five types of fuel cells such as (SOFC), wherein SOFC with respect to other several types of fuel cells also have following some: fuel tolerance is wide, can directly use hydrocarbon polymer to act as a fuel; Adopt all solid state battery structure, efficiently solve problems such as corrosion that liquid electrolyte brings and electrolyte loss; Noble metal electrode need not be used, the production cost of battery can be reduced greatly; Fully utilize the high quality waste heat of discharging, improved the electrical efficiency of battery greatly.Therefore, in the world, the research and development of SOFC more and more are subjected to paying attention to widely.
Well known, the electrochemical catalysis activity of solid oxide fuel cell electrode depends on the microtexture of electrode, and the microtexture of electrode depends on the starting raw material of making electrode and the preparation technology of starting raw material.At present, the method of synthetic perovskite powder material has a lot, for example: solid reaction process, coprecipitation method, spray pyrolysis, sol-gel method, also there is its scabrous problem separately in the starting raw material that still these methods is applied to scale operation high-quality electrode.Though simple as the solid reaction process process, need be under higher temperature of reaction roast and grinding repeatedly for a long time, the component uniformity of the powder that obtains is very poor and sintering activity is low; The coprecipitation method raw materials cost is low, but powder reuniting is more serious, and the stoichiometric ratio of Pb, Sr, Ti is restive in the powder of preparation, and throw out needs repeatedly washing, and technology is complicated; Referring to Fan Zhang, Tomoaki Karaki, Masatoshi Adachi, Synthesis of nanosized (Pb, Sr) TiO
3Perovskite powders by co-precipitation processing, Powder Technology, 159 13-16 (2005).Spray pyrolysis as choose reasonable solvent, temperature of reaction, spray velocity etc., can access the form ultrafine powder different with performance by the red-tape operati condition.Referring to A.Kumar P.S.Devi, A.D.Sharma and H.S.Maiti, " A novel spray-pyrolysis technique to producenanocrystalline lanthanum strontium manganite powder ", J.Am.Ceram.Soc., 88,971-973 (2005); And be the Chinese patent " ammonia complex liquid spray pyrolysis prepares the method and apparatus of basic carbonate nano " of CN1380255A referring to publication number.This operational process of craft is simple, reaction is once finished, can continuous production, and product need not washing, filters and grinds, and avoided unnecessary pollution.But in this technology, nanoparticle adopts special-purpose cyclonic separator just can finish with the needs that separate of gas, and to having relatively high expectations of equipment, and the capture of product is relatively more difficult.In order to overcome the deficiency of this kind spray pyrolysis, publication number is that Chinese patent " spray pyrolysis prepares the method for nano-powder " the employing heat-stable material of CN1235805C is substrate, be covered with the adsorption medium nano carbon black on its surface and solve the capture problem of nano-powder, but such doing increased processing step and increased production cost because of having consumed a large amount of carbon blacks.Though sol-gel method can go out nanometer LSM powder as feedstock production without alkoxide, organic consumption is very big, and production cost is higher, referring to Preparationand characterization of La
1-xSr
xMnO
3+ δ(0≤x≤0.6) powder by sol-gel processing, Manuel Gaudon, Christel Laberty-Robert, Florence Ansart, Philippe Stevens, Abel Rousset, Solid State Sciences 4 (2002) 125-133.
Summary of the invention
At the deficiencies in the prior art, the invention provides a kind of low reunion of suitable scale operation, the preparation method of perovskite structure nano-powder.Prepared nano-powder is as Solid Oxide Fuel Cell (SOFC) cathode material.
Method of the present invention is a raw material with the nitrate solution of La, Co and/or Sr, Fe, stoichiometric ratio according to powder is mixed with mixing solutions, add organic monomer acrylamide and linking agent N, N '-methylene-bisacrylamide stirs the back and adds the initiator ammonium persulfate aqueous solution, heat up, mixing solutions is solidified into gel, and the pre-treatment of dewatering again generates presoma, with the presoma calcining, obtain the powder of perovskite structure.
Method technology of the present invention is simple, need not be raw material with the metal alkoxide, and organic consumption is very low, does not need through steps such as washing and filterings.
The nano-powder general formula of method preparation of the present invention: La
1-xSr
xCo
1-yFe
yO
3, x=0～0.5 wherein, y=0～0.4.
The preparation method of Solid Oxide Fuel Cell (SOFC) cathode material perovskite structure nano-powder, step is as follows:
(1) inorganic raw material is one of following, all prepares by stoichiometric ratio:
The nitrate solution of a, La, Co,
The nitrate solution of b, La, Co, Sr,
The nitrate solution of c, La, Co, Sr, Fe,
Add organic monomer acrylamide (AM) and linking agent N in raw material, N '-methylene-bisacrylamide (MBAM) stirs; Add organic monomer and linking agent total mass be disregard water the nitrate total mass 20～90%;
(2) add initiator ammonium persulfate (APS) aqueous solution, stir, be warming up to 60～80 ℃, the mixing solutions in-situ solidifying becomes gel behind 20～60min;
(3) the gained gel dewaters and pre-treatment under 300～400 ℃, generates presoma;
(4) the gained presoma is calcined between 550～900 ℃, and promptly getting grain size is 20～150 nanometers and the powder that does not have the perovskite structure of other dephasigns.
Preferably, the raw material of described step (1) is saturated nitrate solution.
Preferably, the raw material of described step (1) is La (NO
3)
36H
2O, Co (NO
3)
36H
2O, Sr (NO
3)
2, Fe (NO
3)
39H
2O.
Preferably, the mass ratio of the organic monomer of described step (1) and linking agent is 15～10: 1;
Preferably, the initiator ammonium persulfate aqueous solution of described step (2) is that massfraction is 2～4% the aqueous solution;
Preferably, the add-on of the initiator ammonium persulfate of described step (2) is 1～2% of an organic monomer quality.
Preferably, gained presoma calcining temperature is 600～700 ℃.
Technical characterstic of the present invention is as follows:
1, organic selecting for use: the preferred acrylamide of organic monomer (AM), linking agent are N, N '-methylene-bisacrylamide (MBAM); Organic add-on should be controlled within the specific limits, and very difficult curing of the very few solution of add-on and powder are bigger; Add-on is too much, and the solution curing speed is too fast, has influenced the uniformity coefficient of solution, can cause unnecessary waste simultaneously.Through a large amount of tests, find that surprisingly the total mass of control adds organic monomer and linking agent is inorganic (NO
3)
320 of raw material total mass～80% o'clock can make the different nano-powder of particle diameter.
2, selecting for use of initiator: initiator system of ammonium persulfate of the present invention (APS) is an initiator, and the add-on of initiator also should be controlled within the specific limits, and add-on is very few, and the solution curing speed is very slow even not to be solidified; Add-on is too much, and then the solution too high topical solutions of initiator concentration that do not stir is solidified, has influenced the uniformity coefficient of powder like this.After organic monomer and linking agent mixed, effect was ideal when the add-on of initiator ammonium persulfate APS was organic monomer quality 1～2wt%.
3, presoma calcining: calcining can make carbon and organic compound combustion remaining in the presoma fall on the one hand, makes on the other hand that metal oxide becomes perovskite structure mutually in the presoma.Calcining temperature is controlled between 550～900 ℃.Calcining temperature is low excessively, and perovskite structure changes not exclusively; Calcining temperature is too high, and the particle of perovskite structure nano-powder can be grown up rapidly.
4, the particle diameter of powder is controlled: use method provided by the invention, calcine at 650 ℃, the particle diameter of powder descends along with the increase of organism addition, and the particle diameter of powder is all about 50nm; Presoma is handled 5h down at 900 ℃, and the median size of powder is 150nm.In a word, change organic addition and calcining temperature, the diameter of particle controllable size of the perovskite structure of preparation is between 20～150nm.
The inventive method technology is simple, and constant product quality is a raw material owing to do not need metal alkoxide, and organic consumption is very low, and does not need through steps such as washing and filterings, so raw materials cost and working cost are lower.
The present invention has drawn sol gel process can prepare the advantage that powder crystal grain is less and all even gel injection technology of size distribution is simple to operation, organic content is low etc., and low cost has prepared the less and size distribution of diameter of particle uniformly as the powder of the nano level perovskite structure of SOFC cathode material.
Compared with prior art the present invention's advantage of giving prominence to is:
1. raw material is inorganic salt and common organism, and organic consumption seldom, and production cost is low;
2. presoma need not washing and filtering, and technology is simple, and working cost is low, and calcining temperature is low, less energy consumption;
3. the metering of the element of the A position of perovskite structure and B position is than can strict controlling the product purity height;
4. the particle diameter of powder is controlled.
Description of drawings
Fig. 1 is that the organism addition is La (NO
3)
3And Co (NO
3)
3The XRD curve of the presoma of total mass 80% thermal treatment 2h under differing temps.
Fig. 2 is that the presoma of different organism additions is at the XRD of 650 ℃ of following thermal treatment 2h curve, (a) 20%, (b) 40%, (c) 60%, (d) 80%.
Fig. 3 is that the presoma of different organism additions schemes (a) 20%, (b) 40%, (c) 60%, (d) 80% at the TEM of 650 ℃ of following thermal treatment 2h.
Fig. 4 is that the organism consumption is La (NO
3)
3And Co (NO
3)
360% presoma of total mass is at 900 ℃ of TEM figure that handle 5h gained powders down.
Fig. 5 is that embodiment 2 gained presomas are handled 5h gained La down at 900 ℃
0.6Sr
0.4CoO
3The TEM figure of powder.
Fig. 6 is that embodiment 2 gained presomas are handled 5h gained La down at 900 ℃
0.6Sr
0.4CoO
3The TEM figure of powder.
Fig. 7 is that embodiment 3 gained presomas are handled 5h gained powder La down at 900 ℃
0.6Sr
0.4Co
0.8Fe
0.2O
3The XRD curve.
Fig. 8 is that embodiment 3 gained presomas are handled 5h gained powder La down at 900 ℃
0.6Sr
0.4Co
0.8Fe
0.2O
3TEM figure.
Embodiment
The present invention will be further described below in conjunction with embodiment, but be not limited thereto.
Embodiment 1 different organism additions are to LaCoO
3The influence of particle diameter
La (NO
3)
36H
2O, Co (NO
3)
36H
2O is dissolved in the distilled water, La (NO
3)
36H
2O and Co (NO
3)
36H
2The mol ratio of O is 1: 1, and the massfraction of these two kinds of inorganic salt is 70wt% in the solution; Adding organic monomer in the time of magnetic agitation is acrylamide, and linking agent is N, N '-methylene-bisacrylamide, add organic monomer and linking agent total mass be respectively La (NO
3)
3And Co (NO
3)
320%, 40%, 60% and 80% (wherein the mass ratio of organic monomer and linking agent is 15: 1) of total mass; Continue to stir the solution of 20min to obtain mixing, slowly add the initiator ammonium persulfate aqueous solution then, the consumption of initiator is the 1wt% of monomer mass; In the baking oven with 60～80 ℃ of solution placements after stirring, the mixing solutions in-situ solidifying becomes gel behind 20～60min; The gained gel dewaters and pre-treatment under 300～400 ℃, obtains presoma grey black, loose, cotton-shaped, porous.Wherein the organism addition is La (NO
3)
3And Co (NO
3)
3The presoma of total mass 80% is calcined 2h down at 550 ℃, 600 ℃, 650 ℃, 700 ℃ respectively, and the XRD test result of gained powder as shown in Figure 1.The presoma of different organism consumptions is at 650 ℃ of following thermal treatment 2h, the XRD test result of gained powder as shown in Figure 2, the TEM of powder figure is respectively as shown in Figure 3.The organism consumption is La (NO
3)
3And Co (NO
3)
360% presoma of total mass at 900 ℃ of TEM figure that handle 5h gained powders down as shown in Figure 4.
The adulterated La in embodiment 2 A positions
0.6Sr
0.4CoO
3Powder
La (NO
3)
36H
2O, Sr (NO
3)
2And Co (NO
3)
36H
2O is dissolved in the distilled water, La (NO
3)
36H
2O, Sr (NO
3)
2And Co (NO
3)
36H
2The mol ratio of O is 0.6: 0.4: 1, and the massfraction of these three kinds of inorganic salt is 60.6% in the solution; The adding organic monomer is an acrylamide, and linking agent is N, N '-methylene-bisacrylamide, add organic monomer and linking agent total mass be respectively La (NO
3)
3, Sr (NO
3)
2And Co (NO
3)
380% of total mass; The adding of initiator, the dehydration of gel and pre-treatment are all with embodiment 1.The gained presoma at 900 ℃ of XRD curves of handling down 5h gained powders as shown in Figure 5, the TEM test result is as shown in Figure 6.
Embodiment 3 A positions and B position be adulterated La simultaneously
0.6Sr
0.4Co
0.8Fe
0.2O
3Powder
La (NO
3)
36H
2O, Sr (NO
3)
2, Co (NO
3)
36H
2O and Fe (NO
3)
39H
2O is dissolved in the distilled water, La (NO
3)
36H
2O, Sr (NO
3)
2, Co (NO
3)
36H
2O and Fe (NO
3)
39H
2The mol ratio of O is 0.6: 0.4: 0.8: 0.2, and the massfraction of these four kinds of inorganic salt is 60.2% in the solution; The adding organic monomer is an acrylamide, and linking agent is N, N '-methylene-bisacrylamide, add organic monomer and linking agent total mass be respectively La (NO
3)
3, Sr (NO
3)
2, Co (NO
3)
3And Fe (NO
3)
390% of total mass; The adding of initiator, the dehydration of gel and pre-treatment are all with embodiment 1.The gained presoma at 900 ℃ of XRD curves of handling down 5h gained powders as shown in Figure 7, the TEM test result is as shown in Figure 8.
Claims (8)
1. the preparation method of a solid oxide fuel cell cathode material nanometer powder, nitrate solution with La, Co and/or Sr, Fe is a raw material, stoichiometric ratio according to powder is mixed with mixing solutions, add organic monomer acrylamide and linking agent N, N '-methylene-bisacrylamide, stir the back and add the initiator ammonium persulfate aqueous solution, heat up, mixing solutions is solidified into gel, the gained gel is again through generating presoma after dehydration and the pre-treatment, with the presoma calcining, can obtain the nano-powder of perovskite structure.
2, the preparation method of solid oxide fuel cell cathode material nanometer powder as claimed in claim 1 is characterized in that, the concrete operations step is as follows:
(1) inorganic raw material is one of following, by the stoichiometric ratio preparation:
The nitrate solution of a, La, Co,
The nitrate solution of b, La, Co, Sr,
The nitrate solution of c, La, Co, Sr, Fe,
Add organic monomer acrylamide and linking agent N in raw material, N '-methylene-bisacrylamide stirs; Add organic monomer and linking agent total mass be disregard water the nitrate total mass 20～90%;
(2) add the initiator ammonium persulfate aqueous solution, stir, be warming up to 60～80 ℃, the mixing solutions in-situ solidifying becomes gel behind 20～60min;
(3) the gained gel dewaters and pre-treatment under 300～400 ℃, generates presoma;
(4) the gained presoma is calcined between 550～900 ℃, promptly gets the nano-powder of perovskite structure.
3. by the preparation method of the described solid oxide fuel cell cathode material nanometer powder of claim 1, it is characterized in that described raw material is saturated nitrate solution.
4. by the preparation method of claim 1 or 2 described solid oxide fuel cell cathode material nanometer powders, it is characterized in that described raw material is La (NO
3)
36H
2O, Co (NO
3)
36H
2O, Sr (NO
3)
2Or Fe (NO
3)
39H
2O.
5. by the preparation method of claim 1 or 2 described solid oxide fuel cell cathode material nanometer powders, the mass ratio that it is characterized in that described organic monomer and linking agent is 15～10: 1.
6. by the preparation method of claim 1 or 2 described solid oxide fuel cell cathode material nanometer powders, it is characterized in that the described initiator ammonium persulfate aqueous solution is that massfraction is 2～4% the aqueous solution.
7. by the preparation method of claim 1 or 2 described solid oxide fuel cell cathode material nanometer powders, the add-on that it is characterized in that described initiator ammonium persulfate is 1～2% of an organic monomer quality.
8. by the preparation method of claim 1 or 2 described solid oxide fuel cell cathode material nanometer powders, the grain size that it is characterized in that prepared perovskite structure powder is 20～150 nanometers.
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Cited By (4)
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| CN102616764A (en) * | 2011-10-10 | 2012-08-01 | 山东科技大学 | Preparation method of porous LiFePO4 powder |
| CN108543944A (en) * | 2018-03-13 | 2018-09-18 | 南京师范大学 | The preparation method and its resulting materials of a kind of porous dandelion shape Pd nanodendrites and application |
| CN112289985A (en) * | 2020-09-22 | 2021-01-29 | 合肥国轩高科动力能源有限公司 | C @ MgAl2O4Composite coating modified silicon-based negative electrode material and preparation method thereof |
| CN117080467A (en) * | 2023-07-31 | 2023-11-17 | 河南工业大学 | Hydrogel-based solid electrode material, solid electrode, battery, electrode material and preparation method of solid electrode |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1324740C (en) * | 2005-08-19 | 2007-07-04 | 黑龙江大学 | Solid oxide fuel cell cathode material |
| CN1315211C (en) * | 2005-11-30 | 2007-05-09 | 浙江大学 | Process for preparing fuel battery powder of solid oxide and application |
-
2006
- 2006-12-04 CN CNB2006100705648A patent/CN100447090C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102616764A (en) * | 2011-10-10 | 2012-08-01 | 山东科技大学 | Preparation method of porous LiFePO4 powder |
| CN102616764B (en) * | 2011-10-10 | 2014-04-02 | 山东科技大学 | Preparation method of porous LiFePO4 powder |
| CN108543944A (en) * | 2018-03-13 | 2018-09-18 | 南京师范大学 | The preparation method and its resulting materials of a kind of porous dandelion shape Pd nanodendrites and application |
| CN108543944B (en) * | 2018-03-13 | 2019-11-12 | 南京师范大学 | The preparation method and its resulting materials of a kind of porous dandelion shape Pd nanodendrites and application |
| CN112289985A (en) * | 2020-09-22 | 2021-01-29 | 合肥国轩高科动力能源有限公司 | C @ MgAl2O4Composite coating modified silicon-based negative electrode material and preparation method thereof |
| CN117080467A (en) * | 2023-07-31 | 2023-11-17 | 河南工业大学 | Hydrogel-based solid electrode material, solid electrode, battery, electrode material and preparation method of solid electrode |
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