CN113072056A - Preparation method of metal organic framework derived carbon with high specific surface area - Google Patents
Preparation method of metal organic framework derived carbon with high specific surface area Download PDFInfo
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- 239000012621 metal-organic framework Substances 0.000 title claims abstract description 79
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 52
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims abstract description 32
- 229910001416 lithium ion Inorganic materials 0.000 claims abstract description 32
- 239000000463 material Substances 0.000 claims abstract description 28
- 238000000034 method Methods 0.000 claims abstract description 28
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 18
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 12
- 238000005406 washing Methods 0.000 claims abstract description 11
- WFNRNCNCXRGUKN-UHFFFAOYSA-N 2,3,5,6-tetrafluoroterephthalic acid Chemical compound OC(=O)C1=C(F)C(F)=C(C(O)=O)C(F)=C1F WFNRNCNCXRGUKN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 7
- 238000004140 cleaning Methods 0.000 claims description 15
- 239000011259 mixed solution Substances 0.000 claims description 11
- 238000007654 immersion Methods 0.000 claims description 10
- 239000008367 deionised water Substances 0.000 claims description 9
- 229910021641 deionized water Inorganic materials 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000003763 carbonization Methods 0.000 claims description 8
- 239000007773 negative electrode material Substances 0.000 claims description 8
- 239000000243 solution Substances 0.000 claims description 7
- XIOUDVJTOYVRTB-UHFFFAOYSA-N 1-(1-adamantyl)-3-aminothiourea Chemical compound C1C(C2)CC3CC2CC1(NC(=S)NN)C3 XIOUDVJTOYVRTB-UHFFFAOYSA-N 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 4
- 239000011261 inert gas Substances 0.000 claims description 4
- 238000001291 vacuum drying Methods 0.000 claims description 4
- 238000005303 weighing Methods 0.000 claims description 4
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 238000002791 soaking Methods 0.000 claims 4
- 239000002243 precursor Substances 0.000 abstract description 12
- 238000012360 testing method Methods 0.000 abstract description 7
- 239000002994 raw material Substances 0.000 abstract description 5
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 abstract description 4
- 238000010000 carbonizing Methods 0.000 abstract description 4
- 239000013078 crystal Substances 0.000 abstract description 4
- 229910052731 fluorine Inorganic materials 0.000 abstract description 4
- 239000011737 fluorine Substances 0.000 abstract description 4
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 abstract description 4
- 238000011056 performance test Methods 0.000 abstract description 3
- 239000002904 solvent Substances 0.000 abstract description 3
- 238000012512 characterization method Methods 0.000 abstract 1
- 239000003575 carbonaceous material Substances 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 6
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 description 4
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 4
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 4
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 description 4
- 239000011267 electrode slurry Substances 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 238000001069 Raman spectroscopy Methods 0.000 description 3
- 239000012300 argon atmosphere Substances 0.000 description 3
- 239000010406 cathode material Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 235000019441 ethanol Nutrition 0.000 description 3
- 229910052744 lithium Inorganic materials 0.000 description 3
- -1 lithium hexafluorophosphate Chemical compound 0.000 description 3
- 239000013110 organic ligand Substances 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000001351 cycling effect Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 238000002336 sorption--desorption measurement Methods 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- 238000004438 BET method Methods 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 239000011889 copper foil Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/05—Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
-
- 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
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
- H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
-
- 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
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- General Chemical & Material Sciences (AREA)
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- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
本发明涉及一种具有高比表面积的金属有机框架衍生碳的制备方法，属于电池技术领域。本发明的一种具有高比表面积的金属有机框架衍生碳的制备方法以硝酸锌和四氟对苯二甲酸为前驱体，乙醇作为溶剂，通过水热法合成出一种金属有机框架材料，其中原料中的氟可以用作矿化剂，增加结晶度，促进金属有机框架衍晶体的生长，通过将其高温碳化，并使用盐酸洗涤及后续干燥处理，得到超高比表面积的多孔碳。本发明制备流程简洁，操作简便，表征方便，可将其制备成电极片，组装成CR2032锂离子纽扣电池进行电化学性能测试。当充放电电流密度为0.1A/g时，电池具有1304mAh/g的高比容量。此外，倍率测试和循环测试也体现出良好的电化学性能和优秀的稳定性。
The invention relates to a preparation method of metal-organic framework-derived carbon with high specific surface area, and belongs to the technical field of batteries. A method for preparing a metal-organic framework-derived carbon with high specific surface area of the present invention uses zinc nitrate and tetrafluoroterephthalic acid as precursors and ethanol as a solvent to synthesize a metal-organic framework material by a hydrothermal method, wherein The fluorine in the raw material can be used as a mineralizer to increase crystallinity and promote the growth of metal organic framework derivatized crystals. By carbonizing it at high temperature, washing with hydrochloric acid and subsequent drying, porous carbon with ultra-high specific surface area is obtained. The preparation process of the invention is simple, the operation is simple and the characterization is convenient, and the electrode sheet can be prepared and assembled into a CR2032 lithium ion button battery for electrochemical performance test. When the charge-discharge current density is 0.1 A/g, the battery has a high specific capacity of 1304 mAh/g. In addition, the rate test and cycle test also showed good electrochemical performance and excellent stability.
Description
Technical Field
The invention belongs to the technical field of lithium ion batteries, and particularly relates to a preparation method and application of metal organic framework derived carbon with a high specific surface area.
Background
The lithium ion battery has received a lot of research from people due to its advantages of high specific energy, long cycle life and no environmental pollution, but with the rapid development of various electronic products, the high requirement for the lithium ion battery is increasing day by day. For secondary batteries, the performance of electrode materials influences the development of batteries, and an ideal lithium ion battery cathode material should be capable of accommodating a large amount of lithium ions, and has the characteristics of high ionic conductivity and electronic conductivity, good stability and the like. The graphite is used as a negative electrode material of a commercial lithium ion battery, the theoretical specific capacity of the graphite is only 372mAh/g, and the demand of people on the high-specific-capacity lithium ion battery cannot be met. Therefore, research on the negative electrode material of lithium ion battery with high specific capacity and good cycling stability has become the focus of research.
The metal-organic framework is a novel material in which metal ions and organic compounds are bonded by coordination bonds, and has attracted much attention in recent years. The organic ligand in the metal organic framework is carbonized through a calcination method, metal ions are converted into oxides, and then the oxides are washed away through acid, so that the carbon material with a special morphology can be prepared, and the method becomes a new method for preparing the lithium ion electrode material. Among them, fluorine in the organic raw material may be used as a mineralizer, which not only helps the solvent to dissolve the starting material before the reaction, but also increases the crystallinity and promotes the growth of the metal organic framework crystal. Furthermore, the metal-organic framework derived carbon material has the following characteristics: (1) the carbon obtained after the metal organic framework material with good thermal stability is calcined can well keep a certain shape; (2) as the carbonized organic ligand can be removed in the subsequent calcination and the oxide in the carbonized organic ligand is removed by acid washing, a large amount of pores exist in the prepared carbon material, which is very effective for relieving the volume expansion of the material in the lithium ion storage process and shortening the diffusion path of lithium ions in the material. However, the electrochemical performance of the metal organic framework derived carbon material obtained at present is limited due to insufficient specific surface area.
Disclosure of Invention
The invention aims to solve the technical problems of low specific capacity and poor cycle stability of the conventional lithium ion battery cathode material in the prior art, provides a preparation method of metal organic framework derived carbon with high specific surface area, and applies the metal organic framework derived carbon as the lithium ion battery cathode material to a lithium ion battery. Since the prepared carbon material has large specific surface area, more active sites for lithium ion storage are exposed, and lithium ion diffusion kinetics are reduced, so that high lithium storage and rate performance is realized.
In order to solve the above technical problems, an embodiment of the present invention provides a method for preparing a metal organic framework-derived carbon having a high specific surface area, including the following steps:
(1) weighing 3.856g of zinc nitrate hexahydrate and 1.152g of tetrafluoroterephthalic acid, dissolving in 80mL of absolute ethanol, and stirring to obtain a mixed solution;
(2) carrying out hydrothermal reaction on the mixed solution at 120 ℃ for 12 hours, and then sequentially carrying out immersion cleaning treatment and filtering treatment to obtain a metal organic framework material;
(3) placing the metal organic framework material in a horizontal tube furnace, carrying out carbonization treatment under the condition of continuously introducing inert gas, and then naturally cooling to room temperature to obtain a carbonized product;
(4) sequentially carrying out immersion cleaning treatment, cleaning treatment and filtering treatment on the carbonized product to obtain an acid-cleaned product;
(5) and drying the acid washing product to obtain the metal organic framework derived carbon with high specific surface area.
On the basis of the technical scheme, the invention can be further improved as follows.
Further, the immersion cleaning treatment in the step (2) is specifically immersion cleaning by sequentially using deionized water and absolute ethyl alcohol.
Further, the inert gas is argon.
Further, the carbonization treatment is specifically carried out by heating from room temperature to 800 ℃, and keeping the temperature for 4 hours.
Further, in the carbonization treatment, the temperature rise rate is 5 degrees centigrade per minute.
Further, the immersion cleaning in the step (4) is specifically performed by using a hydrochloric acid solution with a concentration of 20%, and the cleaning is specifically performed by using deionized water for 5 times.
Further, the drying treatment specifically comprises the step of drying the acid-washed product in a vacuum drying oven at 75 ℃ for 24 hours.
Further, the specific surface area of the metal organic framework derived carbon with high specific surface area is 3686m2/g。
In order to solve the technical problem, embodiments of the present invention provide an application of the metal organic framework derived carbon with a high specific surface area as a negative electrode material in the preparation of a lithium ion battery.
The invention has the beneficial effects that: the preparation method of the metal organic framework derived carbon with the high specific surface area uses fluorine in an organic raw material as a mineralizer to quickly prepare the metal organic framework material. The carbon material with ultrahigh specific surface area and pore volume is obtained by processing the metal organic framework in a high-temperature carbonization and acid washing mode, and is applied to the negative electrode of the lithium ion battery. The preparation method is simple and convenient and easy to characterize, and a large number of pores exist in the prepared carbon material with the large specific surface, so that the method is very effective in relieving volume expansion of the material in the lithium ion storage process and shortening the diffusion path of lithium ions in the material, and shows excellent electrochemical performance. When the charge-discharge current density is 0.1A/g, the battery has high specific capacity of 1304mAh/g and also has good rate capability. In addition, under the condition of 5A/g of super-high current density, the specific capacity of 233mAh/g is still kept after 4000 cycles.
Drawings
FIG. 1 is an SEM image of a metal organic framework derived carbon having a high specific surface area according to example 1 of the present invention;
FIG. 2 is a metal organic framework with high specific surface area according to example 1 of the present inventionN of derived carbon2An adsorption-desorption curve;
FIG. 3 is a Raman diagram of a metal-organic framework-derived carbon having a high specific surface area according to example 1 of the present invention;
FIG. 4 is a graph showing the cycle performance at a current density of 5A/g of a metal organic framework-derived carbon having a high specific surface area according to example 1 of the present invention;
FIG. 5 is a graph of rate capability of a metal organic framework-derived carbon having a high specific surface area at different current densities according to an embodiment of the present invention;
fig. 6 is a CV curve of a metal organic framework-derived carbon having a high specific surface area according to an embodiment of the present invention.
Detailed Description
The principles and features of this invention are described below in conjunction with the following drawings, which are set forth by way of illustration only and are not intended to limit the scope of the invention.
Example 1
1.152g of tetrafluoroterephthalic acid and 3.856g of zinc nitrate hexahydrate were dissolved in 80mL of an ethanol solution and uniformly stirred to obtain a mixed solution. And then, carrying out hydrothermal reaction on the mixed solution at 120 ℃ for 12 hours, sequentially using deionized water and absolute ethyl alcohol for immersion cleaning, and filtering to obtain the metal organic framework precursor material. And putting the metal organic framework precursor material into a tube furnace, carbonizing the metal organic framework precursor material for 4 hours at 800 ℃ under the argon atmosphere, cooling the metal organic framework precursor material to room temperature, and taking out the sample. And after taking out, washing the sample for 24 hours by using 20% hydrochloric acid, washing the sample for 5 times by using deionized water, filtering the washed sample, and finally drying the sample in a vacuum drying oven at the temperature of 75 ℃ to obtain the metal organic framework derived carbon with high specific surface area.
In the above examples, the fluorine ion in tetrafluoroterephthalic acid was used as a mineralizer to promote crystallization of the metal-organic framework material; the carbon material containing zinc oxide is produced by the metal organic framework material in the high-temperature carbonization process, and the specific surface area is 3686m by utilizing the reaction of hydrochloric acid and zinc oxide2Carbon material per g.
In order to test the specific capacity, rate capability and cycle performance of the metal organic framework derived carbon with high specific surface area, the metal organic framework derived carbon with high specific surface area is used as a negative electrode in a lithium ion battery to assemble a button battery, and the process is as follows: drying the metal organic framework derived carbon in a vacuum oven at 75 ℃ for 6 hours; then, respectively weighing metal organic framework derived carbon, conductive carbon black and polyvinylidene fluoride according to the mass ratio of 8:1:1, mixing with a proper amount of N-methyl pyrrolidone, grinding into electrode slurry, coating the electrode slurry on an aluminum foil, drying for 24 hours in a vacuum oven at 75 ℃, and cutting into electrode slices with the diameter of 14 mm by using a slicing machine; celgard2400 is used as a separator, metal lithium is used as another electrode, a dimethyl carbonate/diethyl carbonate/ethylene carbonate solution containing 1mol/L lithium hexafluorophosphate is used as an electrolyte, a mixed solution of dimethyl carbonate, diethyl carbonate and ethylene carbonate in a ratio of 1:1:1 is used as a solution, 1mol/L lithium hexafluorophosphate is used as a solute, and the electrolyte and an electrode plate are assembled together to form the lithium-ion button half-cell.
The lithium ion button half cell is subjected to electrochemical performance test on a cell test system of a CT2001A model and an electrochemical workstation of a CH604E model, and the voltage range of the lithium ion button half cell is 0.01-3V.
Fig. 1 is an SEM image of a metal organic framework-derived carbon having a high specific surface area obtained by the method of this example, and it can be seen that the carbon material exhibits a rough porous structure.
Fig. 2 is an N2 adsorption-desorption curve of the metal organic framework-derived carbon with a high specific surface area obtained by the method of the present embodiment, and the curve has a significant hysteresis loop due to the existence of a large number of mesopores; furthermore, the rapid rise of the curve over a small pressure range indicates that the material is rich in a microporous structure; specific surface area of metal organic framework derived carbon found by BET method 3686m2/g。
FIG. 3 is a Raman diagram of the metal-organic framework derived carbon having a high specific surface area obtained by the method of this example, and it can be seen that the Raman diagram is located at 1580cm-1And 1340cm-1The two characteristic peaks in (a) represent that the metal organic framework derived carbon is amorphous carbon.
Fig. 4 shows that the metal organic framework derived carbon with high specific surface area obtained by the method of the present embodiment is used as a lithium ion battery negative electrode active material, and has a cycle performance curve with a current density of 5A/g, and after 4000 cycles, the specific capacity is stabilized at 233mAh/g, and the lithium ion battery negative electrode active material has good cycle stability.
Fig. 5 is a rate performance curve of the metal organic framework derived carbon with high specific surface area obtained by the method of the present embodiment as a negative electrode active material of a lithium ion battery under different current densities, and when the current densities are 0.1, 0.2, 0.5, 1, 2, 5, and 10A/g, the battery has specific capacities of 1304, 1171, 980, 825, 704, 501, and 370mAh/g, and has excellent rate performance.
Fig. 6 is a CV curve measured on an electrochemical workstation of a model CH604E, in which the metal organic framework-derived carbon with high specific surface area obtained by the method of the present embodiment is used as a negative electrode active material of a lithium ion battery, an irreversible peak appears in the first turn due to SEI formation, and the curve maintains a good coincidence in the subsequent tests, indicating that the stability is good.
Comparative example 1
1.152g of terephthalic acid and 3.856g of zinc nitrate hexahydrate were dissolved in 80mL of N, N-dimethylformamide and stirred uniformly to obtain a mixed solution. And then, carrying out hydrothermal reaction on the mixed solution at 120 ℃ for 12 hours, sequentially using deionized water and absolute ethyl alcohol for immersion cleaning, and filtering to obtain the metal organic framework precursor material. And putting the metal organic framework precursor material into a tube furnace, carbonizing the metal organic framework precursor material for 4 hours at 800 ℃ under the argon atmosphere, cooling the metal organic framework precursor material to room temperature, and taking out the sample. And taking out the sample, washing the sample for 24 hours by using 20% hydrochloric acid, washing the sample for 5 times by using deionized water, filtering the sample, and finally drying the sample in a vacuum drying oven at the temperature of 75 ℃ to obtain the metal organic framework derived carbon.
The assembly process of the battery is as follows: respectively weighing metal organic framework derived carbon, conductive carbon black and polyvinylidene fluoride according to the mass ratio of 8:1:1, mixing with a proper amount of N-methyl pyrrolidone, grinding into electrode slurry, coating the electrode slurry on a copper foil, drying in a vacuum oven at 75 ℃ for 24 hours, and cutting into electrode slices with the diameter of 14 mm by using a slicing machine; celgard2400 is used as a diaphragm, metal lithium is used as another electrode, dimethyl carbonate/diethyl carbonate/ethylene carbonate solution containing 1mol/L lithium hexafluorophosphate is used as electrolyte, wherein the volume ratio of dimethyl carbonate, diethyl carbonate and ethylene carbonate is 1:1:1, and the electrolyte and an electrode plate are jointly assembled into the lithium-ion button half-cell.
The processes of comparative example 1 and example 1 are substantially the same, except that comparative example 1 employs a fluorine-free raw material and a co-precipitation method to prepare a metal organic framework-derived carbon. Compared with the metal organic framework derived carbon prepared in example 1, the specific surface area is lower, and the cycling stability is poorer.
Comparative example 2
1.152g of tetrafluoroterephthalic acid and 3.856g of zinc nitrate hexahydrate were dissolved in 80mL of an ethanol solution and uniformly stirred to obtain a mixed solution. And then, carrying out hydrothermal reaction on the mixed solution at 120 ℃ for 12 hours, sequentially using deionized water and absolute ethyl alcohol for immersion cleaning, and filtering to obtain the metal organic framework precursor material. And putting the metal organic framework precursor material into a tubular furnace, and carbonizing at 800 ℃ for 4 hours under an argon atmosphere to obtain the metal organic framework derived carbon.
The process of comparative example 2 is substantially the same as that of example 1 except that comparative example 2 has not been washed with hydrochloric acid. The specific surface area of the metal organic framework derived carbon obtained by the method is 278m2It can be seen that the specific surface area of the metal organic framework derived carbon is greatly reduced without washing with hydrochloric acid.
According to the preparation method of the metal organic framework derived carbon with the high specific surface area, zinc nitrate and tetrafluoroterephthalic acid are used as precursors, ethanol is used as a solvent, a metal organic framework material is synthesized through a hydrothermal method, wherein fluorine in the raw materials can be used as a mineralizer, the crystallinity is increased, the growth of metal organic framework derived crystals is promoted, the metal organic framework derived crystals are carbonized at high temperature, and hydrochloric acid washing and subsequent drying treatment are used to obtain the porous carbon with the ultrahigh specific surface area. The preparation method is simple in preparation process, simple and convenient to operate and convenient to characterize, and the electrode plates can be prepared and assembled into the CR2032 lithium ion button cell for electrochemical performance test. When the charge-discharge current density is 0.1A/g, the battery has high specific capacity of 1304 mAh/g. In addition, the rate test and the cycle test also show good electrochemical performance and excellent stability.
In the description herein, references to the description of the term "one embodiment," "some embodiments," "an example," "a specific example," or "some examples," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (9)
1. A preparation method of metal organic framework derived carbon with high specific surface area is characterized by comprising the following steps:
(1) weighing 3.856g of zinc nitrate hexahydrate and 1.152g of tetrafluoroterephthalic acid, dissolving in 80mL of absolute ethanol, and stirring to obtain a mixed solution;
(2) carrying out hydrothermal reaction on the mixed solution at 120 ℃ for 12 hours, and then sequentially carrying out immersion cleaning treatment and filtering treatment to obtain the metal organic framework material;
(3) placing the metal organic framework material in a horizontal tube furnace, carrying out carbonization treatment under the condition of continuously introducing inert gas, and then naturally cooling to room temperature to obtain a carbonized product;
(4) sequentially carrying out immersion cleaning treatment, cleaning treatment and filtering treatment on the carbonized product to obtain an acid-cleaned product;
(5) and drying the acid washing product to obtain the metal organic framework derived carbon with high specific surface area.
2. The method for preparing the metal organic framework-derived carbon with high specific surface area according to claim 1, wherein the soaking treatment in the step (2) is specifically soaking by sequentially using deionized water and absolute ethyl alcohol.
3. The method for preparing a metal organic framework derived carbon having a high specific surface area according to claim 1, wherein the inert gas is argon.
4. The method for preparing the metal organic framework derived carbon with high specific surface area according to claim 1, wherein the carbonization treatment is specifically raising the temperature from room temperature to 800 ℃ and keeping the temperature for 4 hours.
5. The method for preparing the metal organic framework derived carbon with high specific surface area according to claim 1, wherein the temperature rise rate in the carbonization treatment is 5 degrees centigrade per minute.
6. The method for preparing the metal organic framework derived carbon with high specific surface area according to claim 1, wherein the soaking treatment in the step (4) is soaking by using a 20% hydrochloric acid solution, and the cleaning treatment is cleaning by using deionized water for 5 times.
7. The method for preparing the metal organic framework derived carbon with the high specific surface area according to claim 1, wherein the drying treatment is specifically to dry the acid-washed product in a vacuum drying oven at 75 ℃ for 24 hours.
8. The method for preparing the metal organic framework derived carbon with high specific surface area according to claim 1, wherein the specific surface area of the metal organic framework derived carbon with high specific surface area is 3686m2/g。
9. Use of a metal organic framework derived carbon having a high specific surface area according to any one of claims 1 to 8 as a negative electrode material in the preparation of a lithium ion battery.
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