CN111341980A - A kind of sodium perfluorosulfonate ion battery electrolyte separator and preparation method and application thereof - Google Patents
A kind of sodium perfluorosulfonate ion battery electrolyte separator and preparation method and application thereof Download PDFInfo
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- 239000011734 sodium Substances 0.000 title claims abstract description 50
- 229910052708 sodium Inorganic materials 0.000 title claims abstract description 37
- 239000003792 electrolyte Substances 0.000 title claims abstract description 36
- -1 sodium perfluorosulfonate ion Chemical class 0.000 title claims abstract description 30
- 238000002360 preparation method Methods 0.000 title claims abstract description 28
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000011575 calcium Substances 0.000 claims abstract description 36
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 36
- 239000000463 material Substances 0.000 claims abstract description 17
- 229910001415 sodium ion Inorganic materials 0.000 claims abstract description 16
- 239000012528 membrane Substances 0.000 claims abstract description 12
- 239000003518 caustics Substances 0.000 claims abstract description 9
- 159000000007 calcium salts Chemical class 0.000 claims abstract description 8
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000003513 alkali Substances 0.000 claims abstract description 5
- 150000003463 sulfur Chemical class 0.000 claims abstract description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 51
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical group CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 30
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 claims description 21
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 18
- 239000003292 glue Substances 0.000 claims description 18
- 239000011593 sulfur Substances 0.000 claims description 18
- 229910052717 sulfur Inorganic materials 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 15
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 11
- 239000002002 slurry Substances 0.000 claims description 10
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 9
- 238000005245 sintering Methods 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 8
- 229910001424 calcium ion Inorganic materials 0.000 claims description 8
- 239000006185 dispersion Substances 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 8
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 6
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 6
- 229910052744 lithium Inorganic materials 0.000 claims description 6
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims description 5
- 229910001416 lithium ion Inorganic materials 0.000 claims description 5
- 239000003960 organic solvent Substances 0.000 claims description 5
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 4
- UQSQSQZYBQSBJZ-UHFFFAOYSA-N fluorosulfonic acid Chemical compound OS(F)(=O)=O UQSQSQZYBQSBJZ-UHFFFAOYSA-N 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- XCXLEIPEAAEYTF-UHFFFAOYSA-M sodium fluorosulfate Chemical compound [Na+].[O-]S(F)(=O)=O XCXLEIPEAAEYTF-UHFFFAOYSA-M 0.000 claims description 3
- 229910001413 alkali metal ion Inorganic materials 0.000 claims description 2
- 239000011248 coating agent Substances 0.000 claims description 2
- 238000000576 coating method Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 238000007790 scraping Methods 0.000 claims description 2
- 229910000288 alkali metal carbonate Inorganic materials 0.000 claims 1
- 150000008041 alkali metal carbonates Chemical class 0.000 claims 1
- 159000000013 aluminium salts Chemical class 0.000 claims 1
- 229910000329 aluminium sulfate Inorganic materials 0.000 claims 1
- 229960000935 dehydrated alcohol Drugs 0.000 claims 1
- VEUACKUBDLVUAC-UHFFFAOYSA-N [Na].[Ca] Chemical compound [Na].[Ca] VEUACKUBDLVUAC-UHFFFAOYSA-N 0.000 abstract description 22
- 239000002808 molecular sieve Substances 0.000 abstract description 21
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 abstract description 21
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 abstract description 10
- 210000001787 dendrite Anatomy 0.000 abstract description 9
- 239000002994 raw material Substances 0.000 abstract description 8
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 abstract description 7
- 239000011244 liquid electrolyte Substances 0.000 abstract description 6
- 239000007784 solid electrolyte Substances 0.000 abstract description 3
- 230000001351 cycling effect Effects 0.000 abstract description 2
- 238000001027 hydrothermal synthesis Methods 0.000 abstract description 2
- 229910052751 metal Inorganic materials 0.000 abstract description 2
- 239000002184 metal Substances 0.000 abstract description 2
- 239000000843 powder Substances 0.000 abstract description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 15
- 239000000243 solution Substances 0.000 description 14
- 239000007864 aqueous solution Substances 0.000 description 11
- 230000008569 process Effects 0.000 description 10
- 239000011148 porous material Substances 0.000 description 9
- 239000002131 composite material Substances 0.000 description 8
- 239000013078 crystal Substances 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 6
- PPQREHKVAOVYBT-UHFFFAOYSA-H dialuminum;tricarbonate Chemical compound [Al+3].[Al+3].[O-]C([O-])=O.[O-]C([O-])=O.[O-]C([O-])=O PPQREHKVAOVYBT-UHFFFAOYSA-H 0.000 description 6
- 229910001388 sodium aluminate Inorganic materials 0.000 description 5
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 4
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 4
- 239000007772 electrode material Substances 0.000 description 4
- 238000007086 side reaction Methods 0.000 description 4
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 3
- 229940118662 aluminum carbonate Drugs 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 2
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 150000001340 alkali metals Chemical class 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 150000004645 aluminates Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000004299 exfoliation Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000005562 fading Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000003760 magnetic stirring Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000005518 polymer electrolyte Substances 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- AWRQDLAZGAQUNZ-UHFFFAOYSA-K sodium;iron(2+);phosphate Chemical compound [Na+].[Fe+2].[O-]P([O-])([O-])=O AWRQDLAZGAQUNZ-UHFFFAOYSA-K 0.000 description 1
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/431—Inorganic material
-
- 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
-
- 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
- H01M10/054—Accumulators with insertion or intercalation of metals other than lithium, e.g. with magnesium or aluminium
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/403—Manufacturing processes of separators, membranes or diaphragms
-
- 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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- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
本发明属于钠离子电池固态电解质材料技术领域,具体涉及一种全氟磺酸钠离子电池电解质隔膜及其制备方法和应用。该制备方法以特定比例的钙盐、铝盐和硫盐为原料,通过高温烧结制成硫铝酸钙;再将苛性碱和该硫铝酸钙通过低温水热反应制成含硫铝酸钙钠分子筛;最后将该含硫铝酸钙钠分子筛与PFSA‑Li粉末制备成钠离子固态电解质隔膜。该制备方法制得的成品能减少或避免液体电解质的使用,并显著抑制金属钠负极枝晶的产生,且具有较高的强度,能够作为钠离子二次电池隔膜直接用于组装电池,可显著增强钠离子的电导率和大电流充放电池的循环稳定性。
The invention belongs to the technical field of solid electrolyte materials for sodium ion batteries, and in particular relates to an electrolyte diaphragm of a sodium perfluorosulfonate ion battery and a preparation method and application thereof. The preparation method uses calcium salts, aluminum salts and sulfur salts in specific proportions as raw materials, and is sintered at high temperature to prepare calcium sulfoaluminate; and then the caustic alkali and the calcium sulfoaluminate are made into calcium sulfoaluminate through low-temperature hydrothermal reaction sodium molecular sieve; finally, the sodium ion solid electrolyte membrane is prepared from the calcium sodium sulfoaluminate-containing molecular sieve and PFSA-Li powder. The finished product prepared by the preparation method can reduce or avoid the use of liquid electrolyte, significantly inhibit the generation of dendrites in the metal sodium negative electrode, and has high strength, and can be directly used as a sodium ion secondary battery separator for assembling batteries, which can significantly Enhance the conductivity of sodium ions and the cycling stability of high-current charge-discharge batteries.
Description
技术领域technical field
本发明属于钠离子电池固态电解质材料技术领域,具体涉及一种全氟磺酸钠离子电池电解质隔膜及其制备方法和应用。The invention belongs to the technical field of solid electrolyte materials for sodium ion batteries, and in particular relates to an electrolyte diaphragm of a sodium perfluorosulfonate ion battery and a preparation method and application thereof.
背景技术Background technique
在诸多储能系统中,锂离子电池因能量密度高、功率密度高、放电电压高、自放电率低等众多优点,在便携式设备中得到了飞速发展。然而,锂资源是一种相对稀缺的资源,其大量使用导致锂产品价格节节攀升。钠离子电池虽然能量密度不及锂离子电池,但是由于钠资源丰富易得,在对于能量密度要求不高的领域仍具有良好的应用前景。Among many energy storage systems, lithium-ion batteries have developed rapidly in portable devices due to their high energy density, high power density, high discharge voltage, and low self-discharge rate. However, lithium resource is a relatively scarce resource, and its massive use has led to rising prices of lithium products. Although the energy density of sodium-ion batteries is lower than that of lithium-ion batteries, due to the abundant and easy availability of sodium resources, they still have good application prospects in fields that do not require high energy density.
然而,钠离子电池多采用有机液体电解质,该电解质和电极材料在充放电过程中可对电极材料进行破坏并导致电池容量出现不可逆衰减;同时电池在长期服役过程中,有机液体电解质会出现挥发、干涸、泄漏等现象,严重影响电池寿命。另一方面,由于电极表面电流密度及钠离子分布不均匀等因素,钠离子电池在电池循环中离子的脱出和嵌入会导致电极材料副反应的发生而产生分解产物以及脱落的电极材料,其溶解、沉积可形成不均匀的孔洞和枝晶。枝晶会刺穿隔膜接触正极,造成电池短路、热失控、着火爆炸等一系列安全隐患。However, organic liquid electrolytes are mostly used in sodium-ion batteries, and the electrolytes and electrode materials can damage the electrode materials during the charging and discharging process and cause irreversible attenuation of the battery capacity. Drying, leakage and other phenomena will seriously affect the battery life. On the other hand, due to factors such as the current density on the electrode surface and the uneven distribution of sodium ions, the extraction and insertion of ions during the battery cycle of sodium ion batteries will lead to the occurrence of side reactions in the electrode material, resulting in decomposition products and exfoliated electrode materials. , deposition can form uneven pores and dendrites. The dendrite will pierce the separator and contact the positive electrode, causing a series of safety hazards such as battery short circuit, thermal runaway, fire and explosion.
发明内容SUMMARY OF THE INVENTION
针对液体电解质与电极会发生副反应导致电池容量衰减、枝晶可造成安全隐患的问题,本发明提供一种全氟磺酸钠离子电池电解质隔膜的制备方法。Aiming at the problems that the liquid electrolyte and the electrode will have side reactions, which will cause the battery capacity to decay and dendrites may cause safety hazards, the invention provides a preparation method of an electrolyte separator for a sodium perfluorosulfonate ion battery.
以及,本发明还提供一种全氟磺酸钠离子电池电解质隔膜。And, the present invention also provides an electrolyte separator for sodium perfluorosulfonate ion battery.
以及,本发明还提供上述全氟磺酸钠离子电池电解质隔膜在制备锂离子电池中的应用。And, the present invention also provides the application of the above-mentioned sodium perfluorosulfonate ion battery electrolyte separator in the preparation of lithium ion battery.
为达到上述发明目的,本发明实施例采用了如下技术方案:In order to achieve the above-mentioned purpose of the invention, the embodiment of the present invention adopts the following technical solutions:
一种全氟磺酸钠离子电池电解质隔膜的制备方法,具体包括以下步骤:A preparation method of an electrolyte diaphragm of a sodium perfluorosulfonate ion battery, specifically comprising the following steps:
S1、将钙盐、硫酸盐和铝盐混合,在1300~1600℃烧结,得到多孔层状硫铝酸钙;所述钙盐、硫盐和铝盐中,钙元素与铝元素的摩尔比为1:1.2~2,所述钙元素与硫元素的摩尔比为4~10:1;S1. Mix calcium salt, sulfate and aluminum salt, and sinter at 1300-1600 ° C to obtain porous layered calcium sulfoaluminate; in the calcium salt, sulfur salt and aluminum salt, the molar ratio of calcium element to aluminum element is 1:1.2~2, the molar ratio of the calcium element to the sulfur element is 4~10:1;
S2、将所述多孔层状硫铝酸钙置于苛性碱溶液中,在110~160℃条件下反应;所述苛性碱溶液中的碱金属离子的摩尔量为所述多孔层状硫铝酸钙中钙离子摩尔量的4~10倍;S2, placing the porous layered calcium sulfoaluminate in a caustic alkali solution and reacting at 110-160° C.; the molar amount of alkali metal ions in the caustic solution is the porous layered calcium sulfoaluminate 4 to 10 times the molar amount of calcium ions in calcium;
S3、将S2所得产物与聚氧化乙烯(PEO)、全氟磺酸锂(PFSA-Li)及有机溶剂制成胶液,刮涂后干燥即得。S3, the product obtained in S2 is made into a glue solution with polyethylene oxide (PEO), lithium perfluorosulfonate (PFSA-Li) and an organic solvent, and is dried after scraping.
本发明的制备方法首先在S1中以限定了钙元素、铝元素和硫元素比例的钙盐、铝盐和硫盐为原料,通过特定温度下的高温烧结,可制备得到多孔层状硫铝酸钙。The preparation method of the present invention firstly uses calcium salts, aluminum salts and sulfur salts whose ratios of calcium element, aluminum element and sulfur element are limited as raw materials in S1, and can prepare porous layered sulfoaluminate by high-temperature sintering at a specific temperature calcium.
然后在S2中,S1制得的多孔层状硫铝酸钙与苛性钠中的碱金属通过特定温度的低温水热反应发生离子交换,从而在制得孔径均匀、晶型完整的含硫铝酸钙钠分子筛。该分子筛能够对电极副反应的分解产物及电极脱落物起到选择性的过滤作用,阻止其通过,能够显著抑制金属钠负极枝晶的产生。Then in S2, the porous layered calcium sulfoaluminate prepared in S1 and the alkali metal in caustic soda undergo ion exchange through a low-temperature hydrothermal reaction at a specific temperature, so as to obtain sulfur-containing aluminate with uniform pore size and complete crystal form. Calcium sodium molecular sieve. The molecular sieve can selectively filter the decomposition products of the electrode side reaction and the electrode shedding, prevent them from passing through, and can significantly inhibit the generation of dendrites of the metal sodium negative electrode.
最后,上述含硫铝酸钙钠分子筛在S3中与水溶性PFSA-Li在胶液中通过离子交换反应得到硫铝酸钙钠分子筛改性的PFSA-Na复合物粉末,通过刮涂、干燥后即可形成固态的含硫PFSA-Na复合物隔膜,即全氟磺酸钠离子电池电解质隔膜。PFSA-Li为水溶性,对生产环境要求比较宽松,低温即可成膜,因此S3的反应过程不需要高温和过长的反应时间。S2所得分子筛的骨架结构还能增强该电解质隔膜的强度。Finally, the above-mentioned calcium-sodium sulfoaluminate-containing molecular sieve is ion-exchanged with water-soluble PFSA-Li in S3 to obtain a PFSA-Na composite powder modified by calcium-sodium sulfoaluminate molecular sieve. A solid-state sulfur-containing PFSA-Na composite separator, that is, an electrolyte separator for a sodium perfluorosulfonate ion battery, can be formed. PFSA-Li is water-soluble, and has relatively loose requirements on the production environment, and can form a film at low temperature, so the reaction process of S3 does not require high temperature and long reaction time. The framework structure of the molecular sieve obtained by S2 can also enhance the strength of the electrolyte separator.
与其它聚合物电解质隔膜相比,本发明得到的全氟磺酸钠离子电池电解质隔膜不需要额外添加液体电解质,可直接用于组装电池,导电性能好,不会出现液体电解质与电极发生反应而导致崩塌、熔化等情况,也减少了因液体电解质的使用而导致的电池容量衰减。同时,所得隔膜可过滤电极副反应的分解产物和电极脱落物,可抑制枝晶的产生。将该电解质隔膜作为钠离子二次电池隔膜,能够显著增强钠离子的电导率和大电流充放电池的循环稳定性。Compared with other polymer electrolyte membranes, the perfluorosulfonate sodium ion battery electrolyte membrane obtained by the present invention does not need to add additional liquid electrolyte, can be directly used for assembling batteries, has good electrical conductivity, and will not cause the liquid electrolyte to react with the electrode. Causes collapse, melting, etc., and also reduces battery capacity fading due to the use of liquid electrolytes. At the same time, the obtained separator can filter the decomposition products of the electrode side reaction and the electrode exfoliation, and can suppress the generation of dendrites. Using this electrolyte separator as a separator for sodium ion secondary batteries can significantly enhance the electrical conductivity of sodium ions and the cycle stability of high-current charge-discharge batteries.
本发明制备方法的工艺流程图如图1所示。The process flow diagram of the preparation method of the present invention is shown in FIG. 1 .
优选地,所述混合为将所述钙盐、硫酸盐和铝盐与无水乙醇共同在球磨机中处理至物料混合均匀。Preferably, the mixing is to process the calcium salt, sulfate and aluminum salt together with absolute ethanol in a ball mill until the materials are uniformly mixed.
优选地,所述烧结为在1550~1600℃保温10~15min,再降温至1300~1400℃保温2~10h。Preferably, the sintering is carried out at 1550-1600°C for 10-15 minutes, and then the temperature is lowered to 1300-1400°C for 2-10 hours.
优选地,所述苛性碱为氢氧化钠。Preferably, the caustic is sodium hydroxide.
优选地,所述氢氧化钠溶液的浓度为10~80g/L。在该浓度下,优选反应时间为6~24h。Preferably, the concentration of the sodium hydroxide solution is 10-80 g/L. At this concentration, the preferred reaction time is 6 to 24 hours.
优选地,所述苛性碱溶液中还含有碱金属的碳酸盐,所述碳酸盐中的碳酸根的摩尔量而所述钙元素摩尔量的1/6~1/3。碳酸根能够去除硫铝酸钙中的部分钙,可对硫铝酸钙进一步造孔。Preferably, the caustic alkali solution also contains carbonate of alkali metal, and the molar amount of carbonate in the carbonate is 1/6-1/3 of the molar amount of the calcium element. Carbonate can remove part of calcium in calcium sulfoaluminate, and can further pore for calcium sulfoaluminate.
优选地,所述有机溶剂为二甲基甲酰胺(DMF)。Preferably, the organic solvent is dimethylformamide (DMF).
优选地,制备所述胶液的方法为:将S2所得产物以及所述聚氧化乙烯、全氟磺酸锂和有机溶剂制成浆料,在45~65℃条件下使所述浆料分散至其形成均匀的胶液。Preferably, the method for preparing the glue solution is as follows: the product obtained from S2, the polyethylene oxide, the lithium perfluorosulfonate and the organic solvent are made into a slurry, and the slurry is dispersed to a temperature of 45-65° C. It forms a homogeneous glue.
优选地,所述分散为在磁力搅拌机上分散。在磁力搅拌下,分子筛的正电荷靠近负极磁场,从而得到单向透过性的分子筛,使物质的通过具有选择性。Preferably, the dispersion is on a magnetic stirrer. Under magnetic stirring, the positive charge of the molecular sieve is close to the negative magnetic field, thereby obtaining a molecular sieve with unidirectional permeability, which makes the material pass through selectively.
优选地,所述干燥的温度为80~100℃。Preferably, the drying temperature is 80-100°C.
优选地,所述刮涂的厚度为30~40μm。Preferably, the thickness of the blade coating is 30-40 μm.
以及,本发明实施例还提供一种全氟磺酸钠离子电池电解质隔膜,所述全氟磺酸钠离子电池电解质隔膜是由上述全氟磺酸钠离子电池电解质隔膜的制备方法制备而成。And, the embodiment of the present invention also provides an electrolyte diaphragm of a sodium perfluorosulfonate ion battery, and the electrolyte diaphragm of a sodium perfluorosulfonate ion battery is prepared by the above-mentioned preparation method of an electrolyte diaphragm of a sodium perfluorosulfonate ion battery.
以及,本发明实施例还提供上述全氟磺酸钠离子电池电解质隔膜在制备锂离子电池中的应用。使用上述全氟磺酸钠离子电池电解质隔膜制备成的钠离子电池在多次循环充放电后可保持结构稳定、电池容量不发生明显的衰减,且枝晶能够得到有效抑制。并且以该隔膜组装的电池即使在相对较高的工作温度下仍具有良好的电导率,性能良好。And, the embodiment of the present invention also provides the application of the above-mentioned sodium perfluorosulfonate ion battery electrolyte separator in the preparation of lithium ion battery. The sodium ion battery prepared by using the above-mentioned sodium perfluorosulfonate sodium ion battery electrolyte separator can maintain a stable structure after multiple cycles of charge and discharge, the battery capacity does not experience obvious attenuation, and dendrites can be effectively suppressed. And the battery assembled with the separator still has good conductivity and good performance even at a relatively high working temperature.
附图说明Description of drawings
图1为本发明的工艺流程示意图;Fig. 1 is the process flow schematic diagram of the present invention;
图2为本发明实施例2中S1制得的硫铝酸钙微观形貌;Fig. 2 is the microstructure of calcium sulfoaluminate prepared by S1 in Example 2 of the present invention;
图3为本发明实施例2中S2制得的含硫铝酸钙钠微观形貌。Fig. 3 is the microstructure of calcium sodium aluminate containing sulfur obtained by S2 in Example 2 of the present invention.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合具体实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用于解释本发明,并不用于限定本发明。In order to make the objectives, technical solutions and advantages of the present invention clearer, the present invention will be further described in detail below with reference to specific embodiments. It should be understood that the specific embodiments described herein are only used to explain the present invention, but not to limit the present invention.
实施例1Example 1
本实施例提供了一种全氟磺酸钠离子电池电解质隔膜,其制备方法为:The present embodiment provides a sodium perfluorosulfonate ion battery electrolyte diaphragm, and its preparation method is:
S1、以碳酸钙、硫酸铝和氢氧化铝为原料,按照钙元素、铝元素和硫元素摩尔比为10:17:2的比例进行配料、混合,将混合物料和无水乙醇放入高能球磨机中处理12h,再将处理后的物料制成饼状,放入高温烧结炉中在1600℃烧结10min、降温至1350℃保温6h,制得多孔层状硫铝酸钙。S1, using calcium carbonate, aluminum sulfate and aluminum hydroxide as raw materials, according to the ratio of calcium element, aluminum element and sulfur element molar ratio of 10:17:2, carry out batching and mixing, and put the mixed material and absolute ethanol into the high-energy ball mill After treatment for 12h, the treated material was made into cake shape, put into a high temperature sintering furnace, sintered at 1600°C for 10min, cooled to 1350°C and kept for 6h to obtain porous layered calcium sulfoaluminate.
S2、将S1制得的多孔层状硫铝酸钙放入含有25g/L NaOH水溶液的水热釜中进行钠化和造孔处理,NaOH的摩尔量为多孔层状硫铝酸钙中钙离子摩尔量的6倍,水热温度为135℃,水热时间为8h,制得孔径均匀、晶型完整的含硫铝酸钙钠分子筛。S2, put the porous layered calcium sulfoaluminate obtained from S1 into the hydrothermal kettle containing 25g/L NaOH aqueous solution and carry out sodiumization and pore-forming treatment, and the molar weight of NaOH is the calcium ion in the porous layered calcium sulfoaluminate Molecular weight is 6 times, the hydrothermal temperature is 135℃, and the hydrothermal time is 8h, and the molecular sieve containing calcium sodium aluminate with uniform pore size and complete crystal form is prepared.
S3、将S2制得的含硫铝酸钙钠、PEO、PFSA-Li和DMF制备成浆料,在磁力搅拌机上进行均匀分散,分散过程的温度为55℃,分散12h后形成均匀的胶液。最后将所得胶液进行刮涂(厚度为35μm)后在90℃下干燥8h,制得硫铝酸钙钠分子筛改性的含硫PFSA-Na复合物隔膜。S3. Prepare a slurry containing calcium sodium aluminate, PEO, PFSA-Li and DMF obtained from S2, and uniformly disperse on a magnetic stirrer. The temperature of the dispersion process is 55 °C, and a uniform glue is formed after dispersing for 12 hours. . Finally, the obtained glue solution was scraped (35 μm in thickness) and dried at 90 °C for 8 h to obtain a sulfur-containing PFSA-Na composite membrane modified by calcium sodium sulfoaluminate molecular sieve.
实施例2Example 2
本实施例提供了一种全氟磺酸钠离子电池电解质隔膜,其制备方法为:The present embodiment provides a sodium perfluorosulfonate ion battery electrolyte diaphragm, and its preparation method is:
S1、以碳酸钙、硫酸铝和氢氧化铝为原料,按照钙元素、铝元素和硫元素摩尔比为10:17:2的比例进行配料、混合,将混合物料和无水乙醇放入高能球磨机中处理12h,再将处理后的物料制成饼状,放入高温烧结炉中在1600℃烧结10min、降温至1350℃保温6h,制得多孔层状硫铝酸钙,其微观形貌如图2所示。S1, using calcium carbonate, aluminum sulfate and aluminum hydroxide as raw materials, according to the ratio of calcium element, aluminum element and sulfur element molar ratio of 10:17:2, carry out batching and mixing, and put the mixed material and absolute ethanol into the high-energy ball mill After treatment for 12h, the treated material was made into cake shape, put into a high temperature sintering furnace, sintered at 1600°C for 10min, cooled to 1350°C and kept for 6h to obtain porous layered calcium sulfoaluminate. Its microscopic morphology is shown in the figure. 2 shown.
S2、将S1制得的多孔层状硫铝酸钙放入含有25g/L NaOH水溶液和4.1g/L Na2CO3水溶液的水热釜中进行钠化和造孔处理,NaOH的摩尔量为多孔层状硫铝酸钙中钙离子摩尔量的4倍,水热温度为135℃,水热时间为8h,制得孔径均匀、晶型完整的含硫铝酸钙钠分子筛,其微观形貌如图3所示。S2, the porous layered calcium sulfoaluminate obtained from S1 is put into the hydrothermal still containing 25g/L NaOH aqueous solution and 4.1g/L Na 2 CO 3 aqueous solution to carry out sodiumization and pore-forming treatment, and the molar weight of NaOH is 4 times the molar amount of calcium ions in porous layered calcium sulfoaluminate, the hydrothermal temperature is 135 °C, and the hydrothermal time is 8 h, a molecular sieve containing calcium and sodium sulfoaluminate with uniform pore size and complete crystal form is obtained. Its microscopic morphology As shown in Figure 3.
S3、将S2制得的含硫铝酸钙钠、PEO、PFSA-Li和DMF制备成浆料,在磁力搅拌机上进行均匀分散,分散过程的温度为55℃,分散12h后形成均匀的胶液。最后将所得胶液进行刮涂(厚度为35μm)后在90℃下干燥8h,制得硫铝酸钙钠分子筛改性的含硫PFSA-Na复合物隔膜。S3. Prepare a slurry containing calcium sodium aluminate, PEO, PFSA-Li and DMF obtained from S2, and uniformly disperse on a magnetic stirrer. The temperature of the dispersion process is 55 °C, and a uniform glue is formed after dispersing for 12 hours. . Finally, the obtained glue solution was scraped (35 μm in thickness) and dried at 90 °C for 8 h to obtain a sulfur-containing PFSA-Na composite membrane modified by calcium sodium sulfoaluminate molecular sieve.
实施例3Example 3
本实施例提供了一种全氟磺酸钠离子电池电解质隔膜,其制备方法为:The present embodiment provides a sodium perfluorosulfonate ion battery electrolyte diaphragm, and its preparation method is:
S1、以氢氧化钙、硫酸铝和碳酸铝为原料,按照钙元素、铝元素和硫元素摩尔比为10:15:2的比例进行配料、混合,将混合物料和无水乙醇放入高能球磨机中处理12h,再将处理后的物料制成饼状,放入高温烧结炉中在1550℃烧结15min、降温至1320℃保温4h,制得多孔层状硫铝酸钙。S1. Use calcium hydroxide, aluminum sulfate and aluminum carbonate as raw materials, carry out batching and mixing according to the molar ratio of calcium element, aluminum element and sulfur element as 10:15:2, and put the mixed material and absolute ethanol into the high-energy ball mill After treatment for 12h, the treated material was made into cake shape, put into a high-temperature sintering furnace, sintered at 1550°C for 15min, cooled to 1320°C and kept for 4h to obtain porous layered calcium sulfoaluminate.
S2、将S1制得的多孔层状硫铝酸钙放入含有10g/L NaOH水溶液和0.4g/L Na2CO3水溶液的水热釜中进行钠化和造孔处理,NaOH的摩尔量为多孔层状硫铝酸钙中钙离子摩尔量的10倍,水热温度为160℃,水热时间为6h,制得孔径均匀、晶型完整的含硫铝酸钙钠分子筛。S2, the porous layered calcium sulfoaluminate obtained from S1 is put into a hydrothermal still containing 10g/L NaOH aqueous solution and 0.4g/L Na 2 CO 3 aqueous solution to carry out sodiumization and pore-forming treatment, and the molar weight of NaOH is 10 times the molar amount of calcium ions in the porous layered calcium sulfoaluminate, the hydrothermal temperature is 160 °C, and the hydrothermal time is 6 h, a molecular sieve containing calcium sodium sulfoaluminate with uniform pore size and complete crystal form is prepared.
S3、将S2制得的含硫铝酸钙钠、PEO、PFSA-Li和DMF制备成浆料,在磁力搅拌机上进行均匀分散,分散过程的温度为45℃,分散12h后形成均匀的胶液。最后将所得胶液进行刮涂(厚度为35μm)后在80℃下干燥9h,制得硫铝酸钙钠分子筛改性的含硫PFSA-Na复合物隔膜。S3. Prepare a slurry containing calcium sodium sulfoaluminate, PEO, PFSA-Li and DMF obtained from S2, and uniformly disperse on a magnetic stirrer. The temperature of the dispersion process is 45 °C, and a uniform glue is formed after dispersing for 12 hours. . Finally, the obtained glue solution was scraped (35 μm in thickness) and dried at 80 °C for 9 h to obtain a sulfur-containing PFSA-Na composite membrane modified by calcium sodium sulfoaluminate molecular sieve.
实施例4Example 4
本实施例提供了一种全氟磺酸钠离子电池电解质隔膜,其制备方法为:The present embodiment provides a sodium perfluorosulfonate ion battery electrolyte diaphragm, and its preparation method is:
S1、以硫酸钙、氢氧化钙和碳酸铝为原料,按照钙元素、铝元素和硫元素摩尔比为10:16:2的比例进行配料、混合,将混合物料和无水乙醇放入高能球磨机中处理12h,再将处理后的物料制成饼状,放入高温烧结炉中在1600℃烧结12min、降温至1300℃保温8h,制得多孔层状硫铝酸钙。S1, take calcium sulfate, calcium hydroxide and aluminum carbonate as raw materials, carry out batching and mixing according to the molar ratio of calcium element, aluminum element and sulfur element as 10:16:2, put the mixed material and absolute ethanol into the high-energy ball mill After treatment for 12h, the treated material was made into cake shape, put into a high-temperature sintering furnace, sintered at 1600°C for 12min, cooled to 1300°C and kept for 8h to obtain porous layered calcium sulfoaluminate.
S2、将S1制得的多孔层状硫铝酸钙放入含有30g/L NaOH水溶液和2.5g/L Na2CO3水溶液的水热釜中进行钠化和造孔处理,NaOH的摩尔量为多孔层状硫铝酸钙中钙离子摩尔量的8倍,水热温度为145℃,水热时间为10h,制得孔径均匀、晶型完整的含硫铝酸钙钠分子筛。S2, the porous layered calcium sulfoaluminate obtained from S1 is put into the hydrothermal still containing 30g/L NaOH aqueous solution and 2.5g/L Na 2 CO 3 aqueous solution to carry out sodiumization and pore-forming treatment, and the molar weight of NaOH is The molar amount of calcium ions in the porous layered calcium sulfoaluminate is 8 times, the hydrothermal temperature is 145 °C, and the hydrothermal time is 10 h, and the molecular sieve containing calcium sodium sulfoaluminate with uniform pore size and complete crystal form is prepared.
S3、将S2制得的含硫铝酸钙钠、PEO、PFSA-Li和DMF制备成浆料,在磁力搅拌机上进行均匀分散,分散过程的温度为50℃,分散12h后形成均匀的胶液。最后将所得胶液进行刮涂(厚度为40μm)后在100℃下干燥7h,制得硫铝酸钙钠分子筛改性的含硫PFSA-Na复合物隔膜。S3. Prepare a slurry containing calcium sodium sulfoaluminate, PEO, PFSA-Li and DMF obtained from S2, and uniformly disperse on a magnetic stirrer. The temperature of the dispersion process is 50 °C, and a uniform glue is formed after dispersing for 12 hours. . Finally, the obtained glue solution was scraped (40 μm thick) and dried at 100 °C for 7 h to obtain a sulfur-containing PFSA-Na composite membrane modified by calcium sodium sulfoaluminate molecular sieve.
实施例5Example 5
本实施例提供了一种全氟磺酸钠离子电池电解质隔膜,其制备方法为:The present embodiment provides a sodium perfluorosulfonate ion battery electrolyte diaphragm, and its preparation method is:
S1、以氢氧化钙、硫酸铝和氢氧化铝为原料,按照钙元素、铝元素和硫元素摩尔比为10:12:2.5的比例进行配料、混合,将混合物料和无水乙醇放入高能球磨机中处理12h,再将处理后的物料制成饼状,放入高温烧结炉中在1570℃烧结13min、降温至1350℃保温8h,制得多孔层状硫铝酸钙。S1. Use calcium hydroxide, aluminum sulfate and aluminum hydroxide as raw materials, carry out batching and mixing according to the molar ratio of calcium element, aluminum element and sulfur element as 10:12:2.5, and put the mixed material and absolute ethanol into high-energy After treatment in a ball mill for 12 hours, the treated material was made into a cake shape, placed in a high-temperature sintering furnace, sintered at 1570 °C for 13 minutes, cooled to 1350 °C and kept for 8 hours to obtain porous layered calcium sulfoaluminate.
S2、将S1制得的多孔层状硫铝酸钙放入含有45g/L NaOH水溶液和4.8g/L Na2CO3水溶液的水热釜中进行钠化和造孔处理,NaOH的摩尔量为多孔层状硫铝酸钙中钙离子摩尔量的5倍,水热温度为125℃,水热时间为18h,制得孔径均匀、晶型完整的含硫铝酸钙钠分子筛。S2, the porous layered calcium sulfoaluminate obtained from S1 is put into the hydrothermal still containing 45g/L NaOH aqueous solution and 4.8g/L Na 2 CO 3 aqueous solution to carry out sodiumization and pore-forming treatment, and the molar weight of NaOH is Porous layered calcium sulfoaluminate contains 5 times the molar amount of calcium ions, the hydrothermal temperature is 125 °C, and the hydrothermal time is 18 h, to obtain a calcium-sodium sulfoaluminate molecular sieve with uniform pore size and complete crystal form.
S3、将S2制得的含硫铝酸钙钠、PEO、PFSA-Li和DMF制备成浆料,在磁力搅拌机上进行均匀分散,分散过程的温度为55℃,分散12h后形成均匀的胶液。最后将所得胶液进行刮涂(厚度为35μm)后在95℃下干燥8h,制得硫铝酸钙钠分子筛改性的含硫PFSA-Na复合物隔膜。S3. Prepare a slurry containing calcium sodium aluminate, PEO, PFSA-Li and DMF obtained from S2, and uniformly disperse on a magnetic stirrer. The temperature of the dispersion process is 55 °C, and a uniform glue is formed after dispersing for 12 hours. . Finally, the obtained glue solution was scraped (35 μm in thickness) and dried at 95 °C for 8 h to obtain a sulfur-containing PFSA-Na composite membrane modified by calcium sodium sulfoaluminate molecular sieve.
实施例6Example 6
本实施例提供了一种全氟磺酸钠离子电池电解质隔膜,其制备方法为:The present embodiment provides a sodium perfluorosulfonate ion battery electrolyte diaphragm, and its preparation method is:
S1、以硫酸钙、碳酸钙和碳酸铝为原料,按照钙元素、铝元素和硫元素摩尔比为10:20:1的比例进行配料、混合,将混合物料和无水乙醇放入高能球磨机中处理12h,再将处理后的物料制成饼状,放入高温烧结炉中在1520℃烧结15min、降温至1400℃保温2h,制得多孔层状硫铝酸钙。S1. Use calcium sulfate, calcium carbonate and aluminum carbonate as raw materials, carry out batching and mixing according to the molar ratio of calcium element, aluminum element and sulfur element as 10:20:1, and put the mixed material and absolute ethanol into the high-energy ball mill After treatment for 12h, the treated material was made into cake shape, put into a high temperature sintering furnace, sintered at 1520°C for 15min, cooled to 1400°C and kept for 2h to obtain porous layered calcium sulfoaluminate.
S2、将S1制得的多孔层状硫铝酸钙放入含有80g/L NaOH水溶液和17.7g/L Na2CO3水溶液的水热釜中进行钠化和造孔处理,NaOH的摩尔量为多孔层状硫铝酸钙中钙离子摩尔量的4倍,水热温度为110℃,水热时间为24h,制得孔径均匀、晶型完整的含硫铝酸钙钠分子筛。S2, the porous layered calcium sulfoaluminate obtained from S1 is put into the hydrothermal still containing 80g/L NaOH aqueous solution and 17.7g/L Na 2 CO 3 aqueous solution to carry out sodiumization and pore-forming treatment, and the molar weight of NaOH is The molar amount of calcium ions in the porous layered calcium sulfoaluminate is 4 times, the hydrothermal temperature is 110 °C, and the hydrothermal time is 24 h, and the molecular sieve containing calcium sodium sulfoaluminate with uniform pore size and complete crystal form is prepared.
S3、将S2制得的含硫铝酸钙钠、PEO、PFSA-Li和DMF制备成浆料,在磁力搅拌机上进行均匀分散,分散过程的温度为65℃,分散12h后形成均匀的胶液。最后将所得胶液进行刮涂(厚度为30μm)后在85℃下干燥9h,制得硫铝酸钙钠分子筛改性的含硫PFSA-Na复合物隔膜。S3. Prepare a slurry containing calcium sodium sulfoaluminate, PEO, PFSA-Li and DMF obtained from S2, and uniformly disperse on a magnetic stirrer. The temperature of the dispersion process is 65 °C, and a uniform glue is formed after dispersing for 12 hours. . Finally, the obtained glue solution was scraped (30 μm in thickness) and dried at 85 °C for 9 h to obtain a sulfur-containing PFSA-Na composite membrane modified by calcium sodium sulfoaluminate molecular sieve.
实施例7Example 7
本实施例提供了一种全氟磺酸钠离子电池电解质隔膜在制备钠离子电池中的应用。This embodiment provides an application of an electrolyte separator for a sodium perfluorosulfonate ion battery in the preparation of a sodium ion battery.
以磷酸铁钠为正极、金属钠为负极,用实施例2所得成品为隔膜组装CR2032纽扣电池,测试电压范围为1.2~3.6V。该电池首圈的放电比容量达到128mAh·g-1,性能优异,循环100、500和1000圈后充放电曲线重合度较高,容量保持率分别为99.32%、98.75%和96.58%,极化较小,说明该电池在循环过程中可逆性良好。同时,该组装电池在工作温度为40~50℃时测得的电导率接近10-3S/cm,说明其性能良好。Using sodium iron phosphate as the positive electrode and sodium metal as the negative electrode, and using the finished product obtained in Example 2 as the separator to assemble a CR2032 button battery, the test voltage range is 1.2-3.6V. The discharge specific capacity of the battery in the first cycle reaches 128mAh·g -1 , and the performance is excellent. After 100, 500 and 1000 cycles, the charge-discharge curves have a high degree of overlap, and the capacity retention rates are 99.32%, 98.75%, and 96.58%, respectively. small, indicating that the battery has good reversibility during cycling. At the same time, the measured conductivity of the assembled battery is close to 10 -3 S/cm when the working temperature is 40-50° C., indicating that its performance is good.
循环1000圈后对该组装电池进行拆卸处理,靠近隔膜一侧钠金属负极无明显的钠枝晶生成,靠近正极材料一侧该隔膜上附着微量的10~35nm小颗粒,说明该隔膜能有效抑制枝晶的产生。After 1000 cycles, the assembled battery was disassembled. There was no obvious sodium dendrite formation on the sodium metal negative electrode on the side near the diaphragm, and a small amount of 10-35 nm small particles were attached to the diaphragm on the side near the positive electrode material, indicating that the diaphragm can effectively inhibit Generation of dendrites.
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换或改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent replacements or improvements made within the spirit and principles of the present invention shall be included in the protection of the present invention. within the range.
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