CN113161562A - Defective P3 manganese oxide electro-catalytic material and electro-catalyst - Google Patents
Defective P3 manganese oxide electro-catalytic material and electro-catalyst Download PDFInfo
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- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 title claims abstract description 63
- 230000002950 deficient Effects 0.000 title claims abstract description 50
- 239000000463 material Substances 0.000 title claims abstract description 39
- 239000010411 electrocatalyst Substances 0.000 title claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 11
- 230000007547 defect Effects 0.000 claims abstract description 11
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- 239000000126 substance Substances 0.000 claims abstract description 6
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- QHGJSLXSVXVKHZ-UHFFFAOYSA-N dilithium;dioxido(dioxo)manganese Chemical compound [Li+].[Li+].[O-][Mn]([O-])(=O)=O QHGJSLXSVXVKHZ-UHFFFAOYSA-N 0.000 claims description 17
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 7
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- 229910000016 manganese(II) carbonate Inorganic materials 0.000 claims description 6
- XMWCXZJXESXBBY-UHFFFAOYSA-L manganese(ii) carbonate Chemical compound [Mn+2].[O-]C([O-])=O XMWCXZJXESXBBY-UHFFFAOYSA-L 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- 238000005245 sintering Methods 0.000 claims description 4
- 238000005406 washing Methods 0.000 claims description 4
- 239000011572 manganese Substances 0.000 abstract description 38
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 34
- 239000001301 oxygen Substances 0.000 abstract description 34
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- 239000003054 catalyst Substances 0.000 abstract description 24
- 238000000034 method Methods 0.000 abstract description 18
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- 239000011147 inorganic material Substances 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 18
- 238000006722 reduction reaction Methods 0.000 description 16
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 12
- 229910000473 manganese(VI) oxide Inorganic materials 0.000 description 12
- 239000000243 solution Substances 0.000 description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 8
- 238000012360 testing method Methods 0.000 description 8
- 230000003197 catalytic effect Effects 0.000 description 7
- 239000010410 layer Substances 0.000 description 7
- 239000011259 mixed solution Substances 0.000 description 7
- 239000002243 precursor Substances 0.000 description 7
- 229910052723 transition metal Inorganic materials 0.000 description 7
- 150000003624 transition metals Chemical class 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 6
- 238000000498 ball milling Methods 0.000 description 6
- 239000008367 deionised water Substances 0.000 description 6
- 229910021641 deionized water Inorganic materials 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000000446 fuel Substances 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 238000009210 therapy by ultrasound Methods 0.000 description 6
- 229920000557 Nafion® Polymers 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 239000006229 carbon black Substances 0.000 description 5
- 238000011068 loading method Methods 0.000 description 5
- 239000004570 mortar (masonry) Substances 0.000 description 5
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- 238000011161 development Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000001228 spectrum Methods 0.000 description 4
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 229910021397 glassy carbon Inorganic materials 0.000 description 3
- 229910052744 lithium Inorganic materials 0.000 description 3
- 229910052748 manganese Inorganic materials 0.000 description 3
- PPNAOCWZXJOHFK-UHFFFAOYSA-N manganese(2+);oxygen(2-) Chemical class [O-2].[Mn+2] PPNAOCWZXJOHFK-UHFFFAOYSA-N 0.000 description 3
- 238000002250 neutron powder diffraction Methods 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000012512 characterization method Methods 0.000 description 2
- 230000002153 concerted effect Effects 0.000 description 2
- 238000002484 cyclic voltammetry Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 229910001416 lithium ion Inorganic materials 0.000 description 2
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- 229910052697 platinum Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000004088 simulation Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 229910021642 ultra pure water Inorganic materials 0.000 description 2
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- 241000282414 Homo sapiens Species 0.000 description 1
- 101001018064 Homo sapiens Lysosomal-trafficking regulator Proteins 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 102100033472 Lysosomal-trafficking regulator Human genes 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 235000010703 Modiola caroliniana Nutrition 0.000 description 1
- 244000038561 Modiola caroliniana Species 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- 238000003991 Rietveld refinement Methods 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
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- 230000005713 exacerbation Effects 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
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- 239000012286 potassium permanganate Substances 0.000 description 1
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Images
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/34—Manganese
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/33—Electric or magnetic properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9091—Unsupported catalytic particles; loose particulate catalytic materials, e.g. in fluidised state
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Abstract
The invention provides a defective P3 manganese oxide electrocatalyst, belonging to the field of inorganic materials. The chemical formula of the defect type P3 manganese oxide electrocatalyst provided by the invention is as follows: h1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11. The invention provides an electrocatalyst made of H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11Grinding and mixing with carbon powder. The preparation method is simple and efficient, has mild reaction conditions, is easy to popularize and apply, can provide larger active surface area and more active sites for the contact of the electrolyte and the catalyst, can effectively improve the oxygen reduction activity of the catalyst, can also improve the stability of a layered structure, and can prevent the circulation of the electrolyteThe layered structure is destroyed during the looping process. Meanwhile, oxygen vacancies generated in the acid etching process and the reduced interlayer spacing can be catalyzed cooperatively, so that the oxygen reduction performance of the material is improved.
Description
Technical Field
The invention relates to a defective P3 manganese oxide electro-catalytic material and an electro-catalyst, belonging to the field of inorganic materials.
Background
With the exacerbation of fossil energy crisis and the worsening of ecological environment, the demand of human beings for clean energy storage systems is increasing, and the development and application of new energy conversion and storage systems are important challenges facing the sustainable and healthy development of society. The fuel cell is a clean and efficient hydrogen energy power generation mode, is not limited by Carnot cycle, has high energy conversion efficiency, and can directly convert chemical energy into electric energy. The metal-air battery has high theoretical energy density and great development potential. Both of these two types of batteries with broad prospects for development will undergo oxygen reduction reactions.
The oxygen reduction reaction is an electrochemical process in which oxygen is reduced to hydroxide (alkaline medium) or water (acidic medium) on the cathode surface. Oxygen reduction reactions play a key role in various energy storage and conversion technologies. The reaction kinetics of the process is slow, and the reaction process is complex. At present, the cathode oxygen reduction catalyst is mainly a platinum noble metal catalyst. However, the large-scale application of fuel cells, metal-air cells and the like is severely restricted by the characteristics of scarce platinum reserves, high price, easy poisoning and the like. Therefore, the research for developing the non-noble metal catalyst with high activity, high stability and low cost is very important for the field of electrochemical catalysis.
Manganese oxide is widely concerned by researchers because of the advantages of high abundance of elements, small influence on environment, low cost and the like. Among the various crystal structures of manganese dioxide, layered manganese dioxide has been widely studied because its unique layered structure provides a highly efficient transport path for oxygen reduction reactions. Compared with noble metal catalysts, manganese oxides have limited electronic conductivity and lower oxygen reduction activity, mainly reflected in the overpotential and the ability to catalyze four-electron reduction. Many methods for improving the electrocatalytic activity of manganese oxides have been proposed, such as controlling the nanostructure of manganese oxides, multi-step synthesis increasing active sites, etc., and although these methods are effective, they require complicated synthetic steps or lack long-term stability in air. Therefore, it is necessary to develop a simple method for improving the oxygen reduction activity of manganese oxide.
By utilizing structural transformation to construct a high-performance defective P3 manganese oxide, compared with a precursor, the electro-catalytic material after structural transformation has better electrochemical performance. However, in the field of electrocatalysis, such methods for stabilizing the material structure and changing the intrinsic catalytic activity thereof through structural transformation are rarely reported.
Disclosure of Invention
The present invention has been made to solve the above problems, and an object of the present invention is to provide an oxygen-deficient electrocatalytic material which is simple, efficient, and excellent in universality, and an electrocatalyst containing the electrocatalytic material.
The invention provides a defective P3 manganese oxide electrocatalytic material, which is characterized by the following chemical formula: h1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11□ represents an atomic defect, (abbreviated as HLM).
The defect type P3 manganese oxide electrocatalytic material provided by the invention also has the characteristics that the preparation method comprises the following steps: step 1, stirring and mixing lithium hydroxide and manganese carbonate, and then placing the mixture in a muffle furnace to react for 36-48 h at 400-500 ℃ to obtain layered lithium manganate; step 2, dispersing the layered lithium manganate in a sulfuric acid solution with the concentration of 2M-3M, stirring for 6H-24H at room temperature, washing and drying to obtain H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11。
The defective P3 manganese oxide electrocatalytic material provided by the invention can also be characterized in that the molar ratio of lithium hydroxide to manganese carbonate is (1.8-2.5):1, and preferably 2.05: 1.
The defective P3 manganese oxide electrocatalytic material provided by the present invention may further have a feature that the sintering gas in the muffle furnace in step 1 is air.
The defective P3 manganese oxide electrocatalytic material provided by the invention can also have the characteristic that the sintering temperature in a muffle furnace in the step 1 is 450 ℃.
The deficient P3 manganese oxide electrocatalytic material provided by the invention can also have a characteristic that the concentration of sulfuric acid solution in step 2 is 2.5M.
The defective P3 manganese oxide electrocatalytic material provided by the invention can also have the characteristic that the stirring time at room temperature in the step 2 is 12 h.
The invention also provides an electrocatalyst, characterized by the formula1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11Grinding and mixing with carbon powder.
In the electrocatalyst provided by the invention, there may also be provided a feature wherein H is1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The mass ratio of the carbon powder to the carbon powder is 10 percent to 90 percent to 30 percent to 70 percent.
The electrocatalyst provided by the invention can also have the characteristic that the model of the carbon powder is VulcanXC-72R.
Action and Effect of the invention
According to the defect type P3 manganese oxide electro-catalytic material, the layered O3 type lithium manganate (Li) with mature process and good thermal stability is selected2MnO3) As a precursor, the non-noble metal cathode catalyst with high oxygen reduction activity is prepared by simple acid etching, so the method has the advantages of simple and efficient preparation method, mild reaction conditions, easy popularization and application and the like.
The defect P3 manganese oxide electrocatalytic material is related to because of the defect P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The catalyst has larger specific surface area, so that larger active surface area and more active sites can be provided for the contact of the electrolyte and the catalyst, and the oxygen reduction activity of the catalyst can be effectively improved.
According to the defective P3 manganese oxide electrocatalytic material of the present invention, the lithium is present in the transition metal layer, so that the stability of the layered structure can be improved, and the layered structure can be prevented from being damaged during the cycle. Meanwhile, oxygen vacancies generated in the acid etching process and the reduced interlayer spacing can be catalyzed cooperatively, so that the oxygen reduction performance of the material is improved.
Drawings
FIG. 1 is a schematic structural diagram of a layered lithium manganate precursor of O3 type according to example 1 of the present invention;
FIG. 2 is a schematic structural diagram of a deficient P3 manganese oxide catalytic material in example 1 of the present invention;
FIG. 3 shows example 1 of the present invention (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11) And comparative example 2 (Li)2MnO3) X-ray diffractometer (XRD) to resemble HCrO form P32Is used as a control;
FIG. 4 shows example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The neutron powder diffraction spectrum and the simulation spectrum of (1);
FIG. 5 comparative example 1 (Birnessite-typeMnO)2) An X-ray diffractometer plot;
FIG. 6 shows example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11) Comparison example 1 (Birnessite-typeMnO)2) Comparative example 2 (Li)2MnO3) A graph of oxygen reduction performance for the corresponding samples;
FIG. 7 shows example 1 (defective type)P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11) Comparison example 1 (Birnessite-typeMnO)2) Comparative example 2 (Li)2MnO3) A graph of the percentage of hydrogen peroxide and the number of transferred electrons;
FIG. 8 shows example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11) The prepared catalyst is in a stability chart after 10000 cycles of cyclic voltammetry at the sweep rate of 100 mV/s; and
FIG. 9 shows example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11) Assembled into a performance map of a microfluidic fuel cell.
Detailed Description
In order to make the technical means, the creation features, the achievement purposes and the effects of the invention easy to understand, the invention is specifically described below by combining the embodiment and the attached drawings.
< example 1>
The embodiment provides a defective P3 manganese oxide electrocatalytic material, and the preparation method comprises the following steps:
step 2, preparing 2.5M sulfuric acid solution, and adding 100mg of O3-type layered lithium manganate precursor (Li)2MnO3) Dissolving in 10ml of 2.5M sulfuric acid solution, stirring with magneton at room temperature for 12 hr, centrifuging, washing with ultrapure water and ethanol four times, and drying in vacuum drying oven to obtain defective P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11Which isThe structural formula is shown in figure 2.
FIG. 4 shows example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11) Neutron powder diffraction pattern and fitting pattern.
The data in fig. 4 are refined to verify that Li exists in the transition metal layer and oxygen defects are introduced, so that the construction of the lithium/manganese mixed material structure of the transition metal layer is verified.
< comparative example 1>
The preparation method of the Birnessite-type layered manganese dioxide in the comparative example 1 is as follows:
dissolving 10mmol of potassium permanganate in 65ml of deionized water, stirring with a magneton for 20 minutes to obtain a uniform mauve solution, transferring the solution to a reaction kettle with a Teflon lining, reacting for 48 hours at 220 ℃, after the solution is cooled, centrifugally washing a product with ultrapure water and ethanol for four times, placing the product in a vacuum drying box, and drying to obtain the Birnessite-type layered manganese dioxide.
< comparative example 2>
The comparative example 2 provides O3 type layered lithium manganate, and the preparation method is as follows:
putting 3g of manganese carbonate and 1.28g of anhydrous lithium hydroxide into an agate mortar for grinding, uniformly mixing, putting into a planetary ball milling tank for ball milling at 400rpm for 12 hours, putting the obtained uniform powder into a muffle furnace after ball milling, and reacting for 40 hours at 450 ℃ to obtain reddish brown powder, namely O3 type layered lithium manganate (Li 3 type layered lithium manganate)2MnO3)。
< test example 1>
Characterization by X-ray diffraction
The compounds obtained in example 1 and comparative examples 1 to 2 were subjected to X-ray diffraction. The characterization results are shown in FIGS. 3-5.
FIG. 3 shows an example of the present invention, example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11) And comparative example 2 (Li)2MnO3) X-ray diffractometer (XRD),in the form of HCrO like P32As a control.
As shown in fig. 3, compared to comparative example 2 (Li)2MnO3) Defective P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11After acid treatment, the phase transition occurs and simultaneously the HCrO of P3 type2The structure is similar.
FIG. 4 shows example 1 of the present invention (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11) Neutron powder diffraction experimental spectrum and simulation spectrum.
As shown in FIG. 4, the deficient type P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The structure of (2) is refined by the Rietveld method (Rietveld,1969), but the defect type P3H is obtained after the refinement1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The space group is still C2/m. The refined result shows that atoms Li, H and Mn share the special position of the transition metal layer in the crystallography model, the occupancy rates of Li, H and Mn are respectively 17%, 13% and 67%, and the final chemical formula of the material is H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11Deletion of 0.11O2-. The coincidence between the experimental map and the calculation map after the structure is refined is good.
FIG. 5 comparative example 1 (Birnessite-typeMnO)2) X-ray diffractometer images.
As shown in FIG. 5, comparative example 1 (Birnessite-typeMnO)2) The method is in good agreement with PDF standard card PDF #52-0556, and shows that the synthesized comparative example 1(Birnessite-type MnO)2) Has good compatibility and good crystallinity.
< test example 2>
Testing of catalytic Properties of materials
The defective P3H obtained in example 1 was sampled1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11Adding carbon black (the mass ratio is 30%: 70%) into an oxygen reduction catalyst, grinding the mixture in an agate mortar for 0.5 hour to obtain an electrocatalyst, adding 50 microliter of Nafion (5 wt.%), 1010 microliter of ethanol and 100 microliter of deionized water, carrying out ultrasonic treatment on the mixed solution for 10 minutes by using an ultrasonic cell crusher, uniformly carrying out ultrasonic treatment, coating a proper amount of the mixed solution on the surface of a glassy carbon electrode, obtaining a uniformly covered catalyst film by adopting a rotary drying method, and controlling the defect type P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The loading capacity is 0.12mg/cm2. The catalytic performance of the material was characterized by a rotating disk electrode and an electrochemical workstation.
Adding carbon black (the mass ratio is 30%: 70%) into the Birnessite-type layered manganese dioxide prepared in the comparative example 1, placing the mixture into an agate mortar for grinding for 0.5 hour, adding 50 microliter of Nafion (5 wt.%), 1010 microliter of ethanol and 100 microliter of deionized water, carrying out ultrasonic treatment on the mixed solution for 10 minutes by using an ultrasonic cell crusher, taking a proper amount of the mixed solution after the ultrasonic treatment is uniform, coating the mixed solution on the surface of a glassy carbon electrode, obtaining a uniformly-covered catalyst film by adopting a rotary drying method, and controlling the loading capacity of the Birnessite-type layered manganese dioxide to be 0.12mg/cm2. The catalytic performance of the material was characterized by a rotating disk electrode and an electrochemical workstation.
The O3 type layered lithium manganate (Li) obtained in comparative example 2 was used2MnO3) Adding carbon black (30 mass percent: 70 percent), grinding for 0.5 hour in an agate mortar, adding 50 microliter of Nafion (5 wt.%), 1010 microliter of isopropanol and 100 microliter of deionized water, carrying out ultrasonic treatment on the mixed solution for 10 minutes by using an ultrasonic cell disruptor, uniformly carrying out ultrasonic treatment, coating a proper amount of the mixed solution on the surface of a glassy carbon electrode, obtaining a uniformly-covered catalyst film by adopting a rotary drying method, and controlling O3 type layered lithium manganate (Li 3 type layered lithium manganate)2MnO3) The loading capacity is 0.12mg/cm2. The catalytic performance of the material was characterized by a rotating disk electrode and an electrochemical workstation.
The carbon black used in this test example was VulcanXC-72R.
The test results are shown in FIGS. 6-8.
FIG. 6 shows example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The oxygen reduction polarization curves of the catalysts prepared in the comparative examples 1-2.
As shown in FIG. 6, the deficient type P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11the/C has the maximum limit diffusion current and the minimum overpotential, and the oxygen reduction performance is optimal.
FIG. 7 shows example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The catalyst prepared in comparative examples 1-2 and/C) the percent yield of peroxide by-product and the number of electron transfers.
As shown in FIG. 7, the potential range of 0-0.85Vvs. RHE is for defective P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11C, reaction pathway exhibiting four electrons, reaction by-product HO2-The yield is less than 15%.
FIG. 8 shows example 1 (defective P3H)1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11/C) stability plot of the catalyst after 10000 cycles of cyclic voltammetry at a sweep rate of 100 mV/s.
As shown in FIG. 8, the deficient type P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11the/C showed excellent cycling stability.
< test example 3>
Microfluidic fuel cell performance testing
The defective P3H prepared in example 1 was used1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11Assembled into a microfluidic fuel cell. Taking defective P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11Adding carbon black (30 mass percent: 70 mass percent), mixing with deionized water, isopropanol and Nafion solution uniformly by ultrasonic, spraying on carbon paper as cathode, controlling defective P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The loading capacity is 2.4mg/cm2. Uniformly mixing 20 wt% of Pt/C (Johnson-Matthey) with deionized water, isopropanol and Nafion solution by ultrasonic wave, spraying the mixture on carbon paper to be used as an anode, and controlling the Pt loading amount to be 0.8mg/cm2. 3M potassium hydroxide solution was used as the electrolyte. The microfluidic fuel cell was subjected to performance testing, and the results are shown in fig. 9.
As shown in fig. 9, the catalyst obtained in example 1 has excellent catalytic performance. The defect P3 manganese oxide H provided by the invention1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The oxygen reduction catalyst has larger specific surface area, can provide larger active surface area and more active sites, and can effectively stabilize the layered structure due to the blending of positive tetravalent manganese ions and positive monovalent lithium ions in the transition metal layer, thereby effectively inhibiting the tendency of structural deformation and performance attenuation in the circulation process, and simultaneously, the generation of oxygen vacancies and the reduced interlayer spacing can be subjected to concerted catalysis in the acid etching process, thereby improving the oxygen reduction performance.
Effects and effects of the embodiments
According to the oxygen-deficient electrocatalytic material related to example 1, the layered lithium manganate (Li) with mature process and good thermal stability is selected2MnO3) As a precursor, a non-noble metal cathode catalyst with high oxygen reduction activity is prepared by simple acid etching, so the embodiment 1 has the advantages of simple and efficient preparation method, mild reaction conditions, easy popularization and application and the like.
The oxygen deficient electrocatalytic material according to example 1 is deficient in P3H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11Has large specific surface area, and can be used for electrolysisThe contact of the liquid and the catalyst provides larger active surface area and more active sites, and the oxygen reduction activity of the catalyst can be effectively improved.
According to the oxygen-deficient electrocatalytic material of example 1, since the transition metal layer contains doped lithium, the stability of the layered structure can be improved, and the layered structure can be prevented from being broken during the cycle. Meanwhile, oxygen vacancies generated in the acid etching process and the reduced interlayer spacing can be catalyzed cooperatively, so that the oxygen reduction performance of the material is improved.
The defective P3 manganese oxide electrocatalytic material related to example 1 is due to defective P3 manganese oxide H1.0(H0.13Li0.17□0.03Mn0.67)O1.89□0.11The oxygen reduction catalyst has larger specific surface area, so larger active surface area and more active sites can be provided, and the blending of positive tetravalent manganese ions and positive monovalent lithium ions in the transition metal layer can effectively stabilize the layered structure, effectively inhibit the structural deformation and the tendency of performance attenuation in the circulation process, and simultaneously the generation of oxygen vacancies and the reduced interlayer spacing can be subjected to concerted catalysis in the acid etching process, so the oxygen reduction performance is improved.
The above embodiments are preferred examples of the present invention, and are not intended to limit the scope of the present invention.
Claims (10)
2. The defective P3 manganese oxide electrocatalytic material as set forth in claim 1, wherein the preparation method comprises the steps of:
step 1, stirring and mixing lithium hydroxide and manganese carbonate, and then placing the mixture in a muffle furnace to react for 36-48 h at 400-500 ℃ to obtain layered lithium manganate;
3. The defective P3 manganese oxide electrocatalytic material according to claim 2,
wherein the molar ratio of the lithium hydroxide to the manganese carbonate is (1.8-2.5): 1.
4. The defective P3 manganese oxide electrocatalytic material according to claim 2,
wherein, in the step 1, the sintering gas in the muffle furnace is air.
5. The deficient P3 manganese oxide electrocatalytic material of claim 2, wherein:
wherein the sintering temperature in the muffle furnace in the step 1 is 450 ℃.
6. The deficient P3 manganese oxide electrocatalytic material of claim 2, wherein:
wherein the concentration of the sulfuric acid solution in the step 2 is 2.5M.
7. The deficient P3 manganese oxide electrocatalytic material of claim 2, wherein:
wherein the stirring time at room temperature in the step 2 is 12 h.
10. An electrocatalyst according to claim 8, wherein:
wherein the model of the carbon powder is Vulcan XC-72R.
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