CN113967483A - Application of bimetallic two-dimensional MOF series catalyst to lithium-sulfur battery - Google Patents
Application of bimetallic two-dimensional MOF series catalyst to lithium-sulfur battery Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 52
- JDZCKJOXGCMJGS-UHFFFAOYSA-N [Li].[S] Chemical compound [Li].[S] JDZCKJOXGCMJGS-UHFFFAOYSA-N 0.000 title claims abstract description 32
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 47
- 239000011593 sulfur Substances 0.000 claims abstract description 47
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 47
- 229910052751 metal Inorganic materials 0.000 claims abstract description 39
- 239000002184 metal Substances 0.000 claims abstract description 38
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 19
- -1 polypropylene Polymers 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 15
- 239000003792 electrolyte Substances 0.000 claims abstract description 13
- 238000002360 preparation method Methods 0.000 claims abstract description 13
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 11
- 239000004743 Polypropylene Substances 0.000 claims abstract description 10
- 229920001155 polypropylene Polymers 0.000 claims abstract description 10
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 58
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 54
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims description 33
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 claims description 26
- 238000003756 stirring Methods 0.000 claims description 17
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Chemical class [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 239000006185 dispersion Substances 0.000 claims description 10
- 239000012153 distilled water Substances 0.000 claims description 10
- 238000006386 neutralization reaction Methods 0.000 claims description 10
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 9
- HPNMFZURTQLUMO-UHFFFAOYSA-N diethylamine Chemical compound CCNCC HPNMFZURTQLUMO-UHFFFAOYSA-N 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 9
- 229910017604 nitric acid Inorganic materials 0.000 claims description 9
- 239000000843 powder Substances 0.000 claims description 9
- 238000005406 washing Methods 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 8
- 239000011259 mixed solution Substances 0.000 claims description 8
- 229910052782 aluminium Inorganic materials 0.000 claims description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 7
- 239000011888 foil Substances 0.000 claims description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 6
- 150000003839 salts Chemical class 0.000 claims description 6
- 239000000243 solution Substances 0.000 claims description 6
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- 239000012046 mixed solvent Substances 0.000 claims description 4
- 239000006245 Carbon black Super-P Substances 0.000 claims description 2
- 230000009471 action Effects 0.000 claims description 2
- GFHNAMRJFCEERV-UHFFFAOYSA-L cobalt chloride hexahydrate Chemical compound O.O.O.O.O.O.[Cl-].[Cl-].[Co+2] GFHNAMRJFCEERV-UHFFFAOYSA-L 0.000 claims description 2
- QGUAJWGNOXCYJF-UHFFFAOYSA-N cobalt dinitrate hexahydrate Chemical compound O.O.O.O.O.O.[Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O QGUAJWGNOXCYJF-UHFFFAOYSA-N 0.000 claims description 2
- 239000003273 ketjen black Substances 0.000 claims description 2
- LAIZPRYFQUWUBN-UHFFFAOYSA-L nickel chloride hexahydrate Chemical compound O.O.O.O.O.O.[Cl-].[Cl-].[Ni+2] LAIZPRYFQUWUBN-UHFFFAOYSA-L 0.000 claims description 2
- AOPCKOPZYFFEDA-UHFFFAOYSA-N nickel(2+);dinitrate;hexahydrate Chemical group O.O.O.O.O.O.[Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O AOPCKOPZYFFEDA-UHFFFAOYSA-N 0.000 claims description 2
- 238000009210 therapy by ultrasound Methods 0.000 claims description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims 4
- XKTYXVDYIKIYJP-UHFFFAOYSA-N 3h-dioxole Chemical compound C1OOC=C1 XKTYXVDYIKIYJP-UHFFFAOYSA-N 0.000 claims 2
- XTHFKEDIFFGKHM-UHFFFAOYSA-N Dimethoxyethane Chemical compound COCCOC XTHFKEDIFFGKHM-UHFFFAOYSA-N 0.000 claims 2
- WNXJIVFYUVYPPR-UHFFFAOYSA-N 1,3-dioxolane Chemical compound C1COCO1 WNXJIVFYUVYPPR-UHFFFAOYSA-N 0.000 claims 1
- YCLCFZRBVJIBMF-UHFFFAOYSA-N [Li].FC(F)(F)S(=N)C(F)(F)F Chemical compound [Li].FC(F)(F)S(=N)C(F)(F)F YCLCFZRBVJIBMF-UHFFFAOYSA-N 0.000 claims 1
- 239000012300 argon atmosphere Substances 0.000 claims 1
- 239000003960 organic solvent Substances 0.000 claims 1
- 239000012621 metal-organic framework Substances 0.000 abstract description 69
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 abstract description 18
- 239000000463 material Substances 0.000 abstract description 10
- 229910052786 argon Inorganic materials 0.000 abstract description 9
- 230000008569 process Effects 0.000 abstract description 7
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 238000011161 development Methods 0.000 abstract description 2
- 238000011160 research Methods 0.000 abstract description 2
- 238000003786 synthesis reaction Methods 0.000 abstract description 2
- 238000011946 reduction process Methods 0.000 abstract 2
- 239000012918 MOF catalyst Substances 0.000 description 16
- 238000006243 chemical reaction Methods 0.000 description 13
- 229920001021 polysulfide Polymers 0.000 description 10
- 239000005077 polysulfide Substances 0.000 description 10
- 150000008117 polysulfides Polymers 0.000 description 10
- 230000003197 catalytic effect Effects 0.000 description 9
- 239000012528 membrane Substances 0.000 description 8
- 239000011248 coating agent Substances 0.000 description 6
- 238000000576 coating method Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 229910003473 lithium bis(trifluoromethanesulfonyl)imide Inorganic materials 0.000 description 5
- QSZMZKBZAYQGRS-UHFFFAOYSA-N lithium;bis(trifluoromethylsulfonyl)azanide Chemical compound [Li+].FC(F)(F)S(=O)(=O)[N-]S(=O)(=O)C(F)(F)F QSZMZKBZAYQGRS-UHFFFAOYSA-N 0.000 description 5
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(II) nitrate Inorganic materials [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000013543 active substance Substances 0.000 description 4
- 239000012921 cobalt-based metal-organic framework Substances 0.000 description 4
- 238000011068 loading method Methods 0.000 description 4
- 239000013099 nickel-based metal-organic framework Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000013246 bimetallic metal–organic framework Substances 0.000 description 3
- 239000003575 carbonaceous material Substances 0.000 description 3
- 238000003763 carbonization Methods 0.000 description 3
- 239000000543 intermediate Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229910021580 Cobalt(II) chloride Inorganic materials 0.000 description 2
- 229910001216 Li2S Inorganic materials 0.000 description 2
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 238000000862 absorption spectrum Methods 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002135 nanosheet Substances 0.000 description 2
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000003917 TEM image Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000012876 carrier material Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
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- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/1691—Coordination polymers, e.g. metal-organic frameworks [MOF]
-
- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
- B01J31/223—At least two oxygen atoms present in one at least bidentate or bridging ligand
-
- B01J35/61—
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
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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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
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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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/628—Inhibitors, e.g. gassing inhibitors, corrosion inhibitors
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- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/84—Metals of the iron group
- B01J2531/845—Cobalt
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- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/84—Metals of the iron group
- B01J2531/847—Nickel
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- 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
- Y02E60/10—Energy storage using batteries
Abstract
The invention relates to a preparation method of a bimetallic two-dimensional Metal Organic Framework (MOF) series catalyst and a partitioned series catalysis of the MOF series catalyst on a sulfur reduction process in a lithium sulfur battery, belonging to the technical field of development and research of new energy materials. A small amount of conductive carbon is added in the synthesis process of the MOF, sulfur is loaded, then the conductive carbon is coated on a current collector to serve as a working electrode of a battery, a metal lithium sheet serves as a counter electrode and a reference electrode, a polypropylene film serves as a diaphragm, an organic solution serves as electrolyte, and the button battery is assembled in a glove box filled with high-purity argon. Compared with the prior art, the catalyst can be used as a zoned series catalyst in the electrochemical reduction process of sulfur, is widely applied to the energy field of lithium-sulfur batteries and the like, and has excellent charge/discharge performance.
Description
Technical Field
The invention relates to a preparation method and application of an electrode material, in particular to a preparation method and application of a bimetallic two-dimensional MOF series catalyst, and belongs to the technical field of development and research of new energy materials.
Background
Lithium sulfur batteries have become a powerful candidate for the next generation of high performance energy storage technologies due to their high theoretical energy density and cost effectiveness. However, the electrochemical process of the lithium-sulfur battery is a multi-step conversion reaction, and soluble polysulfide (LiPS) intermediates shuttle between the positive electrode and the negative electrode and react with the lithium negative electrode to generate short-chain polysulfide, so that the active substances of the positive electrode are continuously lost. The shuttling effect ultimately leads to high self-discharge rates, low coulombic efficiencies and poor cycle performance. In addition, the reaction kinetics of the interconversion process of these polysulfide intermediates is slow, resulting in lower power and energy densities of the battery. Based on the challenges, researchers at home and abroad mainly develop a proper anode carrier material, and physical and chemical limitation and chemical adsorption are carried out on the LiPS according to the physicochemical characteristics of the sulfur-carrying material so as to reduce the shuttle effect influence. However, in practical applications, the use of a porous support material or intermediate coating material increases the amount of electrolyte and the volume of the electrode, resulting in a significant decrease in the mass-to-volume ratio and the volumetric energy of the lithium-sulfur battery. Unlike polysulfide adsorption strategies to suppress its diffusion, methods have recently been proposed to accelerate polysulfide conversion using catalyst materials to reduce the effects of shuttling effects. The catalyst material can reduce the energy barrier of the conversion reaction of the LiPS and accelerate the conversion of soluble polysulfide to insoluble end products, thereby solving the problem of enrichment of the soluble LiPS in the electrolyte.
Metal organic framework MOFs have exposed metal sites and open pore structures, which are widely used for storage, catalysis, separation and release of guest molecules. The MOFs are crystal materials formed by metal ion nodes and ligand molecular frameworks through coordination bonds and have periodic structures. Due to the limitation of edge growth, coordinately unsaturated metal sites will reversibly bind to solvent/reactant molecules, which can accelerate polysulfide conversion reactions in lithium sulfur cells. Based on the framework structure of the semiconductor MOF, the metal/nitrogen doped carbon materials obtained by heat treatment and carbonization have been studied more deeply, and the materials (MOF derivatives) have good electronic conductivity, and metal elements keep a monoatomic dispersion or clustering state in a carbon matrix, so the metal/nitrogen doped carbon materials are catalyst materials with excellent performance. The MOF derivative has a plurality of typical applications in the aspect of catalytic conversion of a lithium-sulfur battery, and the utilization rate of active substance sulfur and the energy density of the battery are improved. Although effective, the metal/nitrogen-doped carbon materials prepared by the above-mentioned high-temperature carbonization methods not only require high-temperature (600 ℃ or higher) operation under an inert atmosphere, but also require precise control of synthesis conditions to prevent the growth of metal atom aggregates, thereby being disadvantageous for large-scale utilization.
Lithium sulfur batteries involve solid-liquid-solid heterogeneous conversion, and a single catalytic active center is difficult to meet the requirements of multi-species catalytic conversion in a real battery environment, so that the design of a lithium sulfur battery catalyst has a great challenge. According to the invention, trace conductive carbon is added into the prepared bimetallic two-dimensional MOF, the bimetallic two-dimensional MOF can be used as a lithium-sulfur battery catalyst, and the two-dimensional MOFs has a larger specific surface area and a large number of unsaturated metal sites, so that the bimetallic two-dimensional MOF is an ideal sulfur-carrying catalyst for improving the electrocatalytic performance, and the mass and load transfer process can be accelerated; the bimetal active sites can be connected in series with catalytic liquid-liquid (Li) through strong coupling synergistic effect2S8→Li2S4) And liquid-solid (Li)2S4→Li2S) two areas, which accelerate polysulfide conversion efficiency, inhibit shuttle effect, improve the utilization rate of active substances of conversion reaction, and improve the electrochemical performance of the lithium-sulfur battery.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provide a bimetallic two-dimensional MOF tandem catalyst, a preparation method and application thereof.
The purpose of the invention can be realized by the following technical scheme:
a bimetal two-dimensional MOF series catalyst and a preparation method thereof adopt the following steps:
(1) ultrasonically dispersing Co salt hexahydrate, Ni salt hexahydrate, terephthalic acid and trace conductive carbon in a mixed solvent of distilled water, ethanol and DMF (dimethyl formamide);
(2) adding triethylamine into the solution obtained in the step (1), and uniformly stirring;
(3) and (3) carrying out ultrasonic treatment on the solution obtained in the step (2) at room temperature for a long time, or preparing the bimetal two-dimensional MOF under the microwave action of a microwave reactor, washing the bimetal two-dimensional MOF for a plurality of times by DMF (dimethyl formamide) and ethanol, and drying in vacuum to obtain a bimetal two-dimensional MOF powder sample.
The Co salt hydrate in the step (1) is cobalt nitrate hexahydrate or cobalt chloride hexahydrate, and the Ni salt hydrate is nickel nitrate hexahydrate or nickel chloride hexahydrate; the conductive carbon is mesoporous carbon CMK-3, Ketjen black KB or carbon black Super P; the molar ratio of the Co salt hexahydrate, the Ni salt hexahydrate, the terephthalic acid and the trace conductive carbon is 1:1:2: 2-1: 1:3: 10; the volume ratio of water, ethanol and DMF in the mixed solvent is 1:1: 10-1: 1: 20.
The mole number of the added triethylamine in the step (2) is 5-10 times of that of the terephthalic acid.
The ultrasonic power range in the step (3) is 100-400W, and the ultrasonic time is 5-20 h; or the microwave temperature is 30-40 ℃ and the time is 0.5-2 h.
The application of the bimetallic two-dimensional MOF series catalyst comprises the steps of coating the bimetallic two-dimensional MOF series catalyst on a current collector after sulfur loading to serve as a working electrode of a battery, taking a metal lithium sheet as a counter electrode and a reference electrode, taking a polypropylene membrane as a diaphragm, taking an organic solution as an electrolyte, and assembling the bimetallic two-dimensional MOF series catalyst into the lithium sulfur battery in a glove box filled with high-purity argon.
The sulfur carrying amount of the bimetallic two-dimensional MOF series catalyst is 30-90% by mass; dissolving sulfur in diethylamine, mixing with MOF ethanol dispersion, dropwise adding dilute nitric acid for neutralization, and stirring for 0.5-3 h; the current collector can be an aluminum foil, a carbon-coated aluminum foil, carbon paper or a titanium foil; the electrolyte applied to the lithium-sulfur battery is selected from a mixed solution of 1-6 mol/LLITFSI DME and DOL, wherein the volume of the DME is 1-5 times that of the DOL; the series catalyst refers to bimetallic Ni and Co sites respectively corresponding to lithium-sulfur batteriesAnd catalysis of the conversion reaction.
Lithium sulfur batteries involve solid-liquid-solid heterogeneous conversion, and a single catalytic active center is difficult to meet the requirements of multi-species catalytic conversion in a real battery environment, so that the design of a lithium sulfur battery catalyst has a great challenge. Compared with the prior artCompared with the prior art, the bimetallic two-dimensional MOF series catalyst does not need a high-temperature carbonization step, and the preparation process is simple. According to the invention, trace conductive carbon is added into the bimetal two-dimensional MOF, and the bimetal two-dimensional MOF is prepared by adopting an ultrasonic method or a microwave method and can be used as a series catalyst for chemical reaction of the lithium-sulfur battery sulfur. Wherein the conductive carbon can improve the electronic conductivity of the sulfur electrode, and the bimetallic two-dimensional MOF provides a catalytic active center for polysulfide. The two-dimensional MOFs have larger specific surface area and a large number of unsaturated metal sites, are ideal sulfur-carrying catalysts for improving the electrocatalytic performance, and can accelerate the mass and load transfer process; the bimetal active sites can be connected in series with catalytic liquid-liquid (Li) through strong coupling synergistic effect2S8→Li2S4) And liquid-solid (Li)2S4→Li2S) two areas, which accelerate polysulfide conversion efficiency, inhibit shuttle effect, improve the utilization rate of active substances of conversion reaction, and improve the electrochemical performance of the lithium-sulfur battery. For example, bimetallic two-dimensional MOF catalysts are at 0.1C (1C 1675mAg ═ m ag-1) Under the current density, the specific discharge capacity of the first circle is 1450mAh g-1Is obviously higher than that of a single-metal two-dimensional MOF catalyst.
Drawings
FIG. 1 is a scanning electron microscope photograph of bimetallic two-dimensional MOF nanosheets prepared in example 1;
FIG. 2 is a TEM micrograph of the bimetallic two-dimensional MOF catalyst prepared in example 2 after sulfur loading;
FIG. 3 is an X-ray diffraction pattern of a bimetallic two-dimensional MOF catalyst and sulfur-loaded sample prepared in example 3;
FIG. 4 is a graph of the infrared absorption spectra of the single and bimetallic two-dimensional MOF catalysts prepared in example 4;
FIG. 5 is a linear sweep curve and a Tafel slope curve corresponding to the reduction peak position for the bimetallic two-dimensional MOF catalyst sulfur-loaded anode and the single-metal two-dimensional MOF catalyst sulfur-loaded anode, respectively, prepared in example 5;
fig. 6 is a first charge-discharge curve of the bimetallic two-dimensional MOF catalyst sulfur-loaded anode and the single-metal two-dimensional MOF catalyst sulfur-loaded anode prepared in example 6 at a current density of 0.1C.
Detailed Description
The present invention will be described in detail with reference to specific examples. The following examples will assist those skilled in the art in further understanding the invention, but are not intended to limit the invention in any way. It should be noted that variations and modifications can be made by persons skilled in the art without departing from the spirit of the invention. All falling within the scope of the present invention.
Example 1
The preparation method of the bimetallic two-dimensional MOF series catalyst and the application of the bimetallic two-dimensional MOF series catalyst in the lithium-sulfur battery comprises the following steps:
(1) 0.3mmol of CoCl2·6H2O,0.3mmol NiCl2·6H2O, 0.78mmol of terephthalic acid and 2.5mmol (namely 30mg) of CMK-3 are ultrasonically dispersed in 4mL of distilled water, 4mL of ethanol and 62mL of DMF, 6mmol of triethylamine is added to be uniformly stirred, the mixture is ultrasonically treated for 10h under the power of 200W, DMF and ethanol are respectively subjected to centrifugal washing and vacuum drying at 60 ℃ to obtain a bimetallic MOF two-dimensional powder sample, a scanning electron microscope picture of the sample is shown in figure 1, and the nanosheet prepared by the method is thin and uniform and is transparent.
(2) Carrying sulfur by using a bimetallic two-dimensional MOF series catalyst, wherein the mass percent of the carried sulfur is 30%, dissolving the sulfur in diethylamine, mixing with MOF ethanol dispersion, dropwise adding dilute nitric acid for neutralization, and stirring for 1 h; then coating the carbon paper as a working electrode of the battery, taking a metal lithium sheet as a counter electrode and a reference electrode, taking a polypropylene membrane as a diaphragm, taking a mixed solution of DME and DOL (the volume ratio of DME to DOL is 1:1) of 1mol/LLITFSI as an electrolyte, and assembling the lithium-sulfur battery in a glove box filled with high-purity argon.
Example 2
The preparation method of the bimetallic two-dimensional MOF series catalyst and the application of the bimetallic two-dimensional MOF series catalyst in the lithium-sulfur battery comprises the following steps:
(1) 0.3mmol of CoCl2·6H2O,0.3mmol NiCl2·6H2O, 0.6mmol of terephthalic acid, 0.6mmol of KB in 4mL of distilled water, 4mL of ethanol and 40mL of DMF, ultrasonically dispersing, adding 3mmol of triethylamine, uniformly stirring, ultrasonically treating for 6h at 400W, and respectively passing through DAnd (3) performing centrifugal washing on MF and ethanol, and drying at 60 ℃ in vacuum to obtain a bimetallic two-dimensional MOF powder sample.
(2) Sulfur is carried by a bimetallic two-dimensional MOF series catalyst, the mass percent of the carried sulfur is 90%, the sulfur is dissolved in diethylamine and mixed with MOF ethanol dispersion liquid, stirring time is 3h after dropwise adding dilute nitric acid for neutralization, a transmission electron microscope photo is shown in figure 2, and the sulfur is uniformly distributed on the surface of lamellar bimetallic MOF. Then coating sulfur-loaded bimetallic two-dimensional MOF on a titanium foil to serve as a working electrode of the battery, taking a metal lithium sheet as a counter electrode and a reference electrode, taking a polypropylene membrane as a diaphragm, taking a mixture of DME and DOL (DME and DOL in a volume ratio of 5:1) of 6mol/L LiTFSI as electrolyte, and assembling the lithium-sulfur battery in a glove box filled with high-purity argon.
Example 3
(1) 0.3mmol of Co (NO)3)2·6H2O,0.3mmol Ni(NO3)2·6H2And ultrasonically dispersing 0.9mmol of terephthalic acid and 0.9mmol of Super P in 4mL of distilled water, 4mL of ethanol and 80mL of DMF, adding 3mmol of triethylamine, uniformly stirring, transferring the uniformly mixed solution into a microwave tube, reacting for 0.5h in a microwave reactor at 40 ℃, respectively centrifugally washing by DMF and ethanol, and drying at 60 ℃ in vacuum to obtain a bimetallic two-dimensional MOF powder sample.
(2) The sulfur is carried by a bimetallic two-dimensional MOF series catalyst, the mass percentage of the carried sulfur is 80%, the sulfur is dissolved in diethylamine and mixed with MOF ethanol dispersion liquid, the stirring time is 0.5h after the dropwise addition of dilute nitric acid for neutralization, the X-ray diffraction patterns of the bimetallic two-dimensional MOF before and after the sulfur carrying are shown in figure 3, the fact that the bimetallic MOF is a crystal can be known, and the XRD diffraction peak of the MOF is covered after the high sulfur carrying. Then coating the sulfur-loaded bimetallic two-dimensional MOF on a titanium foil to serve as a working electrode of the battery, taking a metal lithium sheet as a counter electrode and a reference electrode, taking a polypropylene membrane as a diaphragm, taking a mixture of DME and DOL (DME and DOL in a volume ratio of 5:1) of 6mol/LLITFSI as electrolyte, and assembling the lithium-sulfur battery in a glove box filled with high-purity argon.
Example 4
(1) 0.3mmol of Co (NO)3)2·6H2O,0.3mmol Ni(NO3)2·6H2And ultrasonically dispersing 0.7mmol of terephthalic acid and 1.5mmol of Super P in 4mL of distilled water, 4mL of ethanol and 62mL of DMF, adding 7mmol of triethylamine, uniformly stirring, transferring the uniformly mixed solution into a microwave tube, reacting for 2h in a microwave reactor at 30 ℃, respectively centrifugally washing by DMF and ethanol, and drying at 60 ℃ in vacuum to obtain a bimetallic two-dimensional MOF powder sample.
(2) The method comprises the steps of loading sulfur on a bimetallic two-dimensional MOF series catalyst by 60 mass percent, dissolving the sulfur in diethylamine, mixing the sulfur with MOF ethanol dispersion liquid, dropwise adding dilute nitric acid for neutralization, stirring for 2 hours, coating the sulfur-loaded bimetallic two-dimensional MOF on a carbon-coated aluminum foil to serve as a working electrode of a battery, taking a metal lithium sheet as a counter electrode and a reference electrode, taking a polypropylene membrane as a diaphragm, taking a 2mol/L mixture (the volume ratio of DME to DOL is 2:1) of DME and DOL of LiTFSI as electrolyte, and assembling the lithium-sulfur battery in a glove box filled with high-purity argon.
The infrared absorption spectra of the single metal Ni-MOF, the single metal Co-MOF and the double metal two-dimensional MOF catalysts are shown in figure 4, and the single metal MOF and the double metal MOF have the same absorption peaks, which shows that the single metal MOF and the double metal MOF have similar structural frameworks.
Example 5
(1) 0.4mmol of Co (NO)3)2·6H2O,0.4mmol Ni(NO3)2·6H2And ultrasonically dispersing 0.8mmol of terephthalic acid and 4mmol of Super P in 5mL of distilled water, 5mL of ethanol and 60mL of DMF, adding 8mmol of triethylamine, uniformly stirring, transferring the uniformly mixed solution into a microwave tube, reacting for 1h in a microwave reactor at 30 ℃, respectively centrifugally washing by DMF and ethanol, and drying at 60 ℃ in vacuum to obtain a bimetallic two-dimensional MOF powder sample.
(2) Sulfur is carried by a bimetallic two-dimensional MOF series catalyst, the mass percent of the carried sulfur is 70%, the sulfur is dissolved in diethylamine and mixed with MOF ethanol dispersion liquid, diluted nitric acid is dripped for neutralization, the stirring time is 1.5h, then the sulfur-carried bimetallic two-dimensional MOF is coated on aluminum foil to be used as a working electrode of a battery, a metal lithium sheet is used as a counter electrode and a reference electrode, a polypropylene membrane is used as a diaphragm, a 3mol/L mixture (the volume ratio of DME to DOL is 1:1) of DME and DOL of LiTFSI is used as electrolyte, and the lithium-sulfur battery is assembled in a glove box filled with high-purity argon.
The linear sweep rate curve (figure 5a) and tafel slope curve (figures 5b and 5c) of corresponding peak positions after sulfur loading of the single metal Ni-MOF, single metal Co-MOF and bimetallic two-dimensional MOF catalysts and the single metal salt (the sum of the mole numbers of Co and Ni) are added into the catalyst (1) and other experimental steps are invariable. As can be seen from FIG. 5, the comparison of the single metal MOF catalyst, Ni-MOFHas smaller Tafel slope in the conversion process, and Co-MOF is in the process of neutralizationThe conversion reaction has a smaller tafel slope. Namely that bimetallic Ni and Co in bimetallic two-dimensional MOF series catalyst are respectively applied to lithium-sulfur batteries Andplays a role in obvious catalytic conversion.
Example 6
(1) 0.4mmol of Co (NO)3)2·6H2O,0.4mmol Ni(NO3)2·6H2And ultrasonically dispersing 1mmol of terephthalic acid and 1.2mmol of CMK-3 in 5mL of distilled water, 5mL of ethanol and 70mL of DMF, adding 10mmol of triethylamine, uniformly stirring, transferring the uniformly mixed solution into a microwave tube, reacting for 1h at 40 ℃ in a microwave reactor, respectively centrifugally washing with DMF and ethanol, and drying at 60 ℃ in vacuum to obtain a bimetallic two-dimensional MOF powder sample.
(2) Sulfur is carried by a bimetallic two-dimensional MOF series catalyst, the mass percent of the carried sulfur is 60%, the sulfur is dissolved in diethylamine and mixed with MOF ethanol dispersion liquid, diluted nitric acid is dripped for neutralization, the stirring time is 2 hours, then the sulfur-carried bimetallic two-dimensional MOF is coated on carbon paper to be used as a working electrode of a battery, a metal lithium sheet is used as a counter electrode and a reference electrode, a polypropylene membrane is used as a diaphragm, a 2mol/L mixture (the volume ratio of DME to DOL) of LiTFSI and DOL is used as electrolyte, and the lithium sulfur battery is assembled in a glove box filled with high-purity argon.
The single metal salt (the sum of the mole numbers of Co and Ni) is added in the step (1), and the other experimental steps are not changed to prepare the single metal two-dimensional MOF catalyst. After the sulfur is loaded on the single metal Ni-MOF, the single metal Co-MOF and the bimetallic two-dimensional MOF catalyst, when the current density is 0.1C, the first charge-discharge curve is shown in figure 6, and the specific discharge capacity of the first circle of the bimetallic two-dimensional MOF catalyst is 1450mAh g according to figure 6-1Significantly higher than the single metal two-dimensional MOF catalyst.
Example 7
(1) 0.2mmol of Co (NO)3)2·6H2O,0.2mmol Ni(NO3)2·6H2And ultrasonically dispersing 0.6mmol of terephthalic acid and 0.6mmol of KB in 5mL of distilled water, 5mL of ethanol and 60mL of DMF, adding 3mmol of triethylamine, uniformly stirring, ultrasonically treating for 20h at 100W of power, respectively centrifugally washing by DMF and ethanol, and drying at 60 ℃ in vacuum to obtain a bimetallic two-dimensional MOF powder sample.
(2) Sulfur is carried by a bimetallic two-dimensional MOF series catalyst, the mass percent of the carried sulfur is 40%, the sulfur is dissolved in diethylamine and mixed with MOF ethanol dispersion liquid, dilute nitric acid is dripped for neutralization, the stirring time is 1.5h, then the sulfur-carried bimetallic two-dimensional MOF is coated on aluminum foil to be used as a working electrode of a battery, a metal lithium sheet is used as a counter electrode and a reference electrode, a polypropylene membrane is used as a diaphragm, a mixed solution of DME and DOL (DME-DOL volume ratio of 4mol/L LiTFSI) is used as electrolyte, and the lithium-sulfur battery is assembled in a glove box filled with high-purity argon.
The foregoing description of specific embodiments of the present invention has been presented. It is to be understood that the present invention is not limited to the specific embodiments described above, and that various changes and modifications may be made by one skilled in the art within the scope of the appended claims without departing from the spirit of the invention.
Claims (12)
1. A preparation method of a bimetallic two-dimensional MOF tandem catalyst is characterized by comprising the following steps:
(1) ultrasonically dispersing Co salt hexahydrate, Ni salt hexahydrate, terephthalic acid and trace conductive carbon in a mixed solvent of distilled water, ethanol and dimethyl formamide (DMF);
(2) adding triethylamine into the solution obtained in the step (1), and uniformly stirring;
(3) and (3) carrying out ultrasonic treatment on the solution obtained in the step (2) at room temperature for a long time, or preparing the bimetal two-dimensional MOF under the microwave action of a microwave reactor, washing the bimetal two-dimensional MOF for a plurality of times by DMF (dimethyl formamide) and ethanol, and drying in vacuum to obtain a bimetal two-dimensional MOF powder sample.
2. The method for preparing the bimetallic two-dimensional MOF tandem catalyst according to claim 1, wherein the Co salt hydrate in the step (1) is cobalt nitrate hexahydrate or cobalt chloride hexahydrate, and the Ni salt hydrate is nickel nitrate hexahydrate or nickel chloride hexahydrate.
3. The method for preparing the bimetallic two-dimensional MOF tandem catalyst according to claim 1, wherein the conductive carbon in the step (1) is mesoporous carbon CMK-3, Ketjen black KB or carbon black Super P.
4. The preparation method of the bimetallic two-dimensional MOF series catalyst according to claim 1, wherein the molar ratio of Co salt hexahydrate, Ni salt hexahydrate, terephthalic acid and trace conductive carbon in the step (1) is 1:1:2: 2-1: 1:3: 10.
5. The preparation method of the bimetallic two-dimensional MOF series catalyst according to claim 1, wherein the volume ratio of distilled water, ethanol and DMF in the mixed solvent in the step (1) is 1:1: 10-1: 1: 20.
6. The preparation method of the bimetallic two-dimensional MOF tandem catalyst according to claim 1, wherein the molar number of the added triethylamine in the step (2) is 5-10 times that of terephthalic acid.
7. The preparation method of the bimetallic two-dimensional MOF series catalyst according to claim 1, wherein in the step (3), the ultrasonic power is 100-400W, and the ultrasonic time is 5-20 h; or the microwave temperature is 30-40 ℃ and the time is 0.5-2 h.
8. The application of the bimetallic two-dimensional MOF series catalyst as claimed in any one of claims 1 to 7, wherein the bimetallic two-dimensional MOF series catalyst is coated on a current collector as a working electrode of a battery after being carried with sulfur, a metal lithium sheet is a counter electrode and a reference electrode, a polypropylene film is a diaphragm, an organic solution is an electrolyte, and the lithium-sulfur battery is assembled under a high-purity argon atmosphere.
9. The application of the bimetallic two-dimensional MOF series catalyst is characterized in that the sulfur content of the bimetallic two-dimensional MOF series catalyst is 30-90% by mass, the sulfur is dissolved in diethylamine and mixed with MOF ethanol dispersion liquid, and the stirring sulfur-carrying time is 0.5-3 h after the dropwise addition of dilute nitric acid for neutralization.
10. Use of a bimetallic two-dimensional MOF series catalyst according to claim 8, wherein the current collector can be an aluminum foil, a carbon-coated aluminum foil, a carbon paper or a titanium foil.
11. The application of the bimetallic two-dimensional MOF tandem catalyst is characterized in that the organic solvent is selected from a mixed solution of 1-6 mol/L of bis (trifluoromethyl) sulfimide Lithium (LiTFSI) ethylene glycol dimethyl ether (DME) and 1, 3-Dioxolane (DOL), wherein the volume of the DME is 1-5 times of the DOL.
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