CN116031479B - Polymer solid electrolyte slurry and film for lithium ion battery, preparation method and application - Google Patents
Polymer solid electrolyte slurry and film for lithium ion battery, preparation method and application Download PDFInfo
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- 239000007784 solid electrolyte Substances 0.000 title claims abstract description 70
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title claims abstract description 35
- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 35
- 229920000642 polymer Polymers 0.000 title claims abstract description 31
- 239000002002 slurry Substances 0.000 title claims abstract description 30
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- 239000002033 PVDF binder Substances 0.000 claims abstract description 40
- 239000012528 membrane Substances 0.000 claims abstract description 38
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims abstract description 35
- 239000004734 Polyphenylene sulfide Substances 0.000 claims abstract description 34
- 229920000069 polyphenylene sulfide Polymers 0.000 claims abstract description 34
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 23
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 17
- 229910003002 lithium salt Inorganic materials 0.000 claims abstract description 15
- 159000000002 lithium salts Chemical class 0.000 claims abstract description 15
- 239000003960 organic solvent Substances 0.000 claims abstract description 15
- 239000007787 solid Substances 0.000 claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 claims abstract description 7
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 16
- 239000000843 powder Substances 0.000 claims description 11
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 claims description 10
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 9
- 239000006185 dispersion Substances 0.000 claims description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 6
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 6
- 238000004898 kneading Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- 229910013063 LiBF 4 Inorganic materials 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 229910052786 argon Inorganic materials 0.000 claims description 3
- 239000011230 binding agent Substances 0.000 claims description 3
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- UGNWTBMOAKPKBL-UHFFFAOYSA-N tetrachloro-1,4-benzoquinone Chemical compound ClC1=C(Cl)C(=O)C(Cl)=C(Cl)C1=O UGNWTBMOAKPKBL-UHFFFAOYSA-N 0.000 claims description 3
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 239000008139 complexing agent Substances 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims description 2
- 238000002425 crystallisation Methods 0.000 claims description 2
- 230000008025 crystallization Effects 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- -1 tetrachloro-p-benzoquinone anion Chemical class 0.000 claims description 2
- 229910013075 LiBF Inorganic materials 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000010345 tape casting Methods 0.000 claims 1
- 238000001291 vacuum drying Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 5
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- 150000002500 ions Chemical class 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 3
- 210000004027 cell Anatomy 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
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- 238000004832 voltammetry Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000011149 active material Substances 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
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
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- 238000005266 casting Methods 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- UHZZMRAGKVHANO-UHFFFAOYSA-M chlormequat chloride Chemical compound [Cl-].C[N+](C)(C)CCCl UHZZMRAGKVHANO-UHFFFAOYSA-M 0.000 description 1
- 229920000891 common polymer Polymers 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
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- 238000007606 doctor blade method Methods 0.000 description 1
- 239000010408 film Substances 0.000 description 1
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- 238000000227 grinding Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 239000011244 liquid electrolyte Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- DHAFIDRKDGCXLV-UHFFFAOYSA-N n,n-dimethylformamide;1-methylpyrrolidin-2-one Chemical compound CN(C)C=O.CN1CCCC1=O DHAFIDRKDGCXLV-UHFFFAOYSA-N 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000005518 polymer electrolyte Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 229910001251 solid state electrolyte alloy Inorganic materials 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Classifications
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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
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Abstract
Description
技术领域Technical field
本发明属于锂离子电池材料领域,涉及一种锂离子电池聚合物固态电解质浆料、膜、制备方法及应用。The invention belongs to the field of lithium-ion battery materials and relates to a lithium-ion battery polymer solid electrolyte slurry, membrane, preparation method and application.
背景技术Background technique
固态锂离子电池具有能量密度高、体积小、安全、柔性可变形的应用前景而备受关注。Solid-state lithium-ion batteries have attracted much attention due to their high energy density, small size, safety, flexibility and deformability.
固态锂离子电池的关键材料是固态电解质,包括聚合物体系(电导率10-7-10-5S/cm)、氧化物体系(电导率10-6-10-3S/cm)、硫化物体系(电导率10-3-10-2S/cm);与传统液态电解质(电导率10-2S/cm)相比具有较低的电导率。而且在电芯中应用时,由于电极、电解质的固/固界面接触面积小,界面阻抗较高,锂离子在界面之间的传输受阻,这就直接导致了固态锂电池存在着阻抗高,倍率差,循环不稳定的问题,限制了其应用。The key material of solid-state lithium-ion batteries is solid electrolyte, including polymer system (conductivity 10 -7 -10 -5 S/cm), oxide system (conductivity 10 -6 -10 -3 S/cm), sulfide system (conductivity 10 -3 -10 -2 S/cm); compared with traditional liquid electrolytes (conductivity 10 -2 S/cm), it has lower conductivity. Moreover, when used in batteries, due to the small solid/solid interface contact area of electrodes and electrolytes, the interface impedance is high, and the transmission of lithium ions between the interfaces is blocked. This directly leads to the high impedance and high rate of solid-state lithium batteries. Poor and unstable circulation limits its application.
聚合物固态电解质则具有较好的柔性和易加工性能,与电极界面接触性好,可以降低固态电池的界面电阻;另外,材料低的密度,可以增加电池的能量密度,在全固态锂金属负极电池中受到越来越多的关注。常见的聚合物固态电解质聚偏氟乙烯(PVDF)类聚合物因为具有稳定的电化学性能和机械性能,并能够很好的解离锂盐以提升其电导率而受到重视。但其具有较高的结晶度,结晶区域占比高,导致锂离子在PVDF晶体结构内无法快速传输,在室温下离子传导能力差,约10-5S·cm-1,一般通过采用凝胶化的方法来改善其导电性能,而这又会导致机械性能的下降。张等报道了基于PVDF–LiX的固态电解质膜,在25 °C 的室温下电导率达到了2.03 × 10−4S cm−1 (X. Zhang, S. Wang, C. Xue, C. Xin, Y.Lin, Y. Shen, L. Li, C.-W. Nan, Adv. Mater. 2019, 31, 1806082.)。尽管这促进了全固态锂金属电池的发展。但是PVDF基固态电解质膜仍然存在的力学性能、热稳定性以及与电极界面相容性差的问题,仍然需要进一步的改善其性能以满足商业化固态锂电池生产的需求。Polymer solid-state electrolytes have good flexibility and easy processing properties, and have good contact with the electrode interface, which can reduce the interface resistance of solid-state batteries. In addition, the low density of the material can increase the energy density of the battery. In all-solid-state lithium metal anodes Batteries are receiving more and more attention. Common polymer solid electrolyte polyvinylidene fluoride (PVDF) polymers have attracted attention because of their stable electrochemical and mechanical properties and their ability to well dissociate lithium salts to improve their conductivity. However, it has a high degree of crystallinity and a high proportion of crystalline areas, which results in the inability to transport lithium ions quickly within the PVDF crystal structure. It has poor ion conductivity at room temperature, about 10 -5 S·cm -1 . Generally, it is achieved by using a gel. Chemical methods are used to improve its electrical conductivity, which in turn leads to a decrease in mechanical properties. Zhang et al. reported a solid electrolyte membrane based on PVDF–LiX with a conductivity of 2.03 × 10 −4 S cm −1 at room temperature of 25 °C (X. Zhang, S. Wang, C. Xue, C. Xin, Y. Lin, Y. Shen, L. Li, C.-W. Nan, Adv. Mater. 2019, 31, 1806082.). Although this promotes the development of all-solid-state lithium metal batteries. However, PVDF-based solid electrolyte membranes still have problems with poor mechanical properties, thermal stability, and poor interface compatibility with electrodes, and their performance still needs to be further improved to meet the needs of commercial solid-state lithium battery production.
发明内容Contents of the invention
本发明针对PVDF基固态电解质界面接触较差,固/固界面阻抗高,锂离子在界面之间的传输受阻,室温离子电导率低,力学性能差等问题,在改善界面问题的基础上仍然要兼具高容量、高能量密度以及高安全性的要求,提出了一种可以将固态电解质浆料,能够部分替换或全部替换制作电芯的过程中使用的单一的PVDF粘结剂,从而起到增大锂离子传输效率,改善界面接触,降低界面阻抗的作用。This invention aims at the problems of poor interface contact of the PVDF-based solid electrolyte, high solid/solid interface impedance, blocked transmission of lithium ions between the interfaces, low room temperature ionic conductivity, poor mechanical properties, etc. On the basis of improving the interface problems, the invention still needs to In order to meet the requirements of high capacity, high energy density and high safety, a solid electrolyte slurry is proposed that can partially or completely replace the single PVDF binder used in the process of making battery cells, thereby achieving Increase lithium ion transmission efficiency, improve interface contact, and reduce interface impedance.
另外,针对PVDF结晶度高、离子电导率低、力学性能差的问题,提供了一种固态电解质膜及其制备方法,通过加入预锂化的聚苯硫醚改善PVDF的结晶度,提高固态电解质膜的力学性能;通过硫醚键上的S位通道提高定向锂离子迁移,提升离子电导率,同时,起到锂离子整流效应,有效抑制锂枝晶生长的作用。In addition, in order to solve the problems of high crystallinity, low ionic conductivity and poor mechanical properties of PVDF, a solid electrolyte membrane and its preparation method are provided. By adding pre-lithiated polyphenylene sulfide, the crystallinity of PVDF is improved and the solid electrolyte is improved. Mechanical properties of the membrane; through the S-site channel on the thioether bond, it improves directional lithium ion migration and improves ionic conductivity. At the same time, it plays a lithium ion rectification effect and effectively inhibits the growth of lithium dendrites.
以及上述固态电解质浆料、固态电解质膜在锂离子二次电池中的应用。and the application of the above-mentioned solid electrolyte slurry and solid electrolyte membrane in lithium-ion secondary batteries.
本发明的技术方案如下:The technical solution of the present invention is as follows:
一种锂离子电池聚合物固态电解质浆料的制备方法,其特征在于,包括以下步骤:A method for preparing lithium-ion battery polymer solid electrolyte slurry, which is characterized by including the following steps:
步骤S1:预锂化聚苯硫醚粉体制备,将聚苯硫醚颗粒、氯化锂与四氯对苯醌阴离子络合剂进行混合,置于氩气或氮气的反应釜中升温至200-400℃,反应2-5h,随后1-2℃/分控温冷却至室温,得到的产物用去离子水多次洗涤并抽滤至中性,60℃真空干燥12-24h,得到预锂化聚苯硫醚粉料A;Step S1: Preparation of prelithiated polyphenylene sulfide powder. Mix polyphenylene sulfide particles, lithium chloride and tetrachloro-p-benzoquinone anionic complexing agent, and place them in an argon or nitrogen reactor and heat it to 200°C. -400℃, react for 2-5h, and then cool to room temperature with 1-2℃/min temperature control. The obtained product is washed with deionized water several times and filtered until neutral, and vacuum dried at 60℃ for 12-24h to obtain pre-lithium Polyphenylene sulfide powder A;
步骤S2:聚合物固态电解质浆料的制备,将步骤S1中得到的预锂化的聚苯硫醚粉体A与聚偏氟乙烯(PVDF)在行星搅拌机或混捏机中预混1-2h,缓慢加入有机溶剂至固含量40-60%之间,进行半干法混捏1-5h,直至物料捏合均匀;加入锂盐,继续混捏1-5h后,再加入有机溶剂至固含量10-30%进行高速分散混合,分散速度2000-5000转/分,分散时间1-2h,得到固态电解质浆料B。Step S2: Preparation of polymer solid electrolyte slurry, pre-mix the prelithiated polyphenylene sulfide powder A obtained in step S1 and polyvinylidene fluoride (PVDF) in a planetary mixer or kneader for 1-2 hours, Slowly add the organic solvent until the solid content is between 40-60%, and perform semi-dry kneading for 1-5 hours until the materials are evenly kneaded; add lithium salt, continue kneading for 1-5 hours, and then add the organic solvent until the solid content is 10-30%. Carry out high-speed dispersion and mixing with a dispersion speed of 2000-5000 rpm and a dispersion time of 1-2 hours to obtain solid electrolyte slurry B.
进一步地,步骤S1中所述聚苯硫醚、氯化锂和四氯对苯醌的质量比为100:5-15:15-50。Further, the mass ratio of polyphenylene sulfide, lithium chloride and tetrachloro-p-benzoquinone described in step S1 is 100:5-15:15-50.
进一步地,所述聚偏氟乙烯(PVDF)、预锂化聚苯硫醚粉料A、锂盐的用量为40-50重量份、10-20重量份、20-40重量份。Further, the amounts of polyvinylidene fluoride (PVDF), prelithiated polyphenylene sulfide powder A, and lithium salt are 40-50 parts by weight, 10-20 parts by weight, and 20-40 parts by weight.
进一步地,所述锂盐为LiBF4和LiODFB构成的复盐,所述复盐中LiBF4与LiODFB的质量比为1﹕1~1.5。Further, the lithium salt is a double salt composed of LiBF 4 and LiODFB, and the mass ratio of LiBF 4 to LiODFB in the double salt is 1:1 to 1.5.
进一步地,所述有机溶剂为N,N-二甲基甲酰胺、四氢呋喃、N-甲基吡咯烷酮(NMP)中的一种或几种。Further, the organic solvent is one or more of N,N-dimethylformamide, tetrahydrofuran, and N-methylpyrrolidone (NMP).
所述的离子电池聚合物固态电解质浆料制备方法制备的离子电池聚合物固态电解质浆料。The ion battery polymer solid electrolyte slurry prepared by the described ion battery polymer solid electrolyte slurry preparation method.
所述离子电池聚合物固态电解质浆料的应用,其特征在于,在制作电芯的过程中用于电芯极片的粘结剂,完全或部分替换单一的PVDF粘结剂。The application of the ion battery polymer solid electrolyte slurry is characterized by completely or partially replacing a single PVDF binder with the binder used for the battery core pole pieces in the process of making the battery core.
基于所述的固态电解质浆料制备锂离子电池聚合物固态电解质膜的方法,其特征在于,采用刮涂机利用流延的方法将所述固态电解质浆料B涂膜成厚度为25μm-50μm的固态电解质膜,放入温度为60-100℃的真空烘箱中干燥10-24小时,最终得到固态电解质膜C。A method for preparing a lithium-ion battery polymer solid electrolyte membrane based on the solid electrolyte slurry, which is characterized in that the solid electrolyte slurry B is coated into a film with a thickness of 25 μm-50 μm by using a doctor blade coating machine and a casting method. The solid electrolyte membrane is placed in a vacuum oven at a temperature of 60-100°C to dry for 10-24 hours, and finally the solid electrolyte membrane C is obtained.
所述锂离子电池聚合物固态电解质膜的方法制备的锂离子电池聚合物固态电解质膜,其特征在于,由连续相聚偏氟乙烯(PVDF)、增强相预锂化聚苯硫醚(PPS)、锂盐以及有机溶剂组成,其中PVDF的质量百分含量为40%-50%,预锂化PPS的质量百分含量为10%-20%,锂盐的质量百分含量为20-40%,有机溶剂的百分含量为5-15%。The lithium ion battery polymer solid electrolyte membrane prepared by the method of the lithium ion battery polymer solid electrolyte membrane is characterized in that it is composed of continuous phase polyvinylidene fluoride (PVDF), reinforced phase prelithiated polyphenylene sulfide (PPS), It consists of lithium salt and organic solvent, in which the mass percentage of PVDF is 40%-50%, the mass percentage of pre-lithiated PPS is 10%-20%, and the mass percentage of lithium salt is 20-40%. The percentage content of organic solvent is 5-15%.
进一步地,锂离子电池聚合物固态电解质膜中,所述连续相PVDF分子结构的结晶度<72%;所述聚苯硫醚的线性结晶区大于90%。Further, in the lithium-ion battery polymer solid electrolyte membrane, the crystallinity of the continuous phase PVDF molecular structure is <72%; the linear crystallization zone of the polyphenylene sulfide is greater than 90%.
所述的固态电解质膜在制备电芯中的应用,其特征在于,放置在正电极和负电极之间,制作金属锂负极锂离子电池或无负极锂离子电池。The application of the solid electrolyte membrane in the preparation of battery cells is characterized by being placed between the positive electrode and the negative electrode to produce a lithium metal negative electrode lithium ion battery or a negative electrode lithium ion battery.
与现有技术相比,本发明具有以下优势Compared with the existing technology, the present invention has the following advantages
制得的聚合物固态电解质浆料可以部分或全部替代PVDF粘结剂,减小电极/电解质界面的接触电阻,降低电池极化内阻、对电池的循环和性能的稳定发挥起到有益效果。The prepared polymer solid electrolyte slurry can partially or completely replace the PVDF binder, reduce the contact resistance at the electrode/electrolyte interface, reduce the polarization internal resistance of the battery, and play a beneficial role in the cycle and stable performance of the battery.
增强相预锂化聚苯硫醚的加入,可以提高PVDF固态电解质膜的力学强度,同时增强离子导电率,由于预锂化聚苯硫醚具有的螯合剂可以螯合阴离子,防止浓差极化,提高锂离子沿着硫(S)位通道进行定向迁移,达到锂离子整流效应,从而有效抑制锂枝晶的生长。The addition of reinforcing phase pre-lithiated polyphenylene sulfide can improve the mechanical strength of the PVDF solid electrolyte membrane and enhance the ionic conductivity. The chelating agent of pre-lithiated polyphenylene sulfide can chelate anions and prevent concentration polarization. , improve the directional migration of lithium ions along the sulfur (S) site channel to achieve the lithium ion rectification effect, thereby effectively inhibiting the growth of lithium dendrites.
所制得的聚合物固态电解质膜具有分解电压高,锂离子迁移数大,离子电导率高的优点,可以有效提高锂金属负极电池的电化学性能,以满足商业化固态锂电池应用的要求。The prepared polymer solid electrolyte membrane has the advantages of high decomposition voltage, large lithium ion migration number, and high ionic conductivity. It can effectively improve the electrochemical performance of lithium metal anode batteries to meet the requirements of commercial solid-state lithium battery applications.
提供了一种简单高效的方法来制备聚合物固态电解质膜,通过简单共混的方法,使得制膜工艺简单,成膜快,效率高,所用常规设备易于控制操作,从而能够大批量制备聚合物固态电解质及膜,满足商业化固态锂电池生产的需求。Provides a simple and efficient method to prepare polymer solid electrolyte membranes. Through a simple blending method, the membrane production process is simple, the membrane formation is fast, and the efficiency is high. The conventional equipment used is easy to control and operate, so that polymers can be prepared in large quantities. Solid electrolytes and membranes meet the needs of commercial solid-state lithium battery production.
附图说明Description of the drawings
图1是实施例1中聚合物固态电解质膜的实物图;Figure 1 is a physical diagram of the polymer solid electrolyte membrane in Example 1;
图2是实施例1中聚合物固态电解质膜的SEM图;Figure 2 is an SEM image of the polymer solid electrolyte membrane in Example 1;
图3是实施例1聚合物固态电解质的拉伸性能图;Figure 3 is a tensile performance diagram of the polymer solid electrolyte of Example 1;
图4是实施例1聚合物固态电解质的分解电压(LSV)图。Figure 4 is a decomposition voltage (LSV) diagram of the polymer solid electrolyte of Example 1.
实施方式Implementation
以下几个实例是对于本发明具体实验操作部分的一个说明,只用于说明本发明,不能理解为对本发明的限制。The following examples are an illustration of the specific experimental operation part of the present invention. They are only used to illustrate the present invention and cannot be understood as limiting the present invention.
实施例Example
先将聚苯硫醚颗粒50g、氯化锂5g与四氯对苯醌15g进行混合,置于连续通入氩气的反应釜中升温至220℃,反应3h,随后控制1℃/分降温冷却至室温,得到的产物用去离子水多次洗涤并抽滤至中性,60℃真空干燥20h,得到预锂化聚苯硫醚粉料A。First, mix 50g of polyphenylene sulfide particles, 5g of lithium chloride and 15g of tetrachloro-p-benzoquinone, place it in a reaction kettle that continuously supplies argon gas, raise the temperature to 220°C, react for 3 hours, and then control the cooling at 1°C/min. to room temperature, the obtained product was washed multiple times with deionized water, filtered until neutral, and vacuum dried at 60°C for 20 hours to obtain prelithiated polyphenylene sulfide powder A.
将聚偏氟乙烯(PVDF)放入烘箱80℃干燥24小时,然后取50g PVDF和9.2g预锂化的聚苯硫醚粉体A,在行星搅拌机中预混2h,缓慢加入100 mL N-甲基吡咯烷酮(NMP),半干混捏2h,然后按质量比1﹕1.2加入33g LiBF4和LiODFB组成的复盐,继续混捏2h后,再加入有机溶剂250 mL NMP,设定分散速度3000转/分,分散时间1h,进行高速分散混合,得到固态电解质浆料B。Put polyvinylidene fluoride (PVDF) into an oven to dry at 80°C for 24 hours, then take 50g PVDF and 9.2g pre-lithiated polyphenylene sulfide powder A, premix them in a planetary mixer for 2h, and slowly add 100 mL N- Methyl pyrrolidone (NMP), semi-dry knead for 2 hours, then add 33g of double salt composed of LiBF 4 and LiODFB at a mass ratio of 1:1.2, continue kneading for 2 hours, then add 250 mL of organic solvent NMP, and set the dispersion speed to 3000 rpm/ minutes, dispersion time is 1 hour, and high-speed dispersion and mixing is performed to obtain solid electrolyte slurry B.
在刮涂机上将固态电解质浆料B涂覆成厚度为30μm的薄膜,然后放置于真空烘箱,100℃干燥24小时,得到聚合物固态电解质膜C,见图1。使用扫描电子显微镜SEM可以观察到固态电解质膜的表面,见图2,可以观察到PPS均匀分布在PVDF的连续相中。使用交流阻抗法测量固态电解质膜电导率为2.82×10-4 S/cm。使用电子万能试验机测得拉伸强度为6MPa,见图3,锂片/固态电解质膜/钢片半电池线性伏安法测试电化学窗口4 .5V,线性伏安曲线见图4所示。The solid electrolyte slurry B is coated on a blade coater into a thin film with a thickness of 30 μm, and then placed in a vacuum oven and dried at 100°C for 24 hours to obtain the polymer solid electrolyte membrane C, as shown in Figure 1. The surface of the solid electrolyte membrane can be observed using a scanning electron microscope (SEM), as shown in Figure 2. It can be observed that PPS is evenly distributed in the continuous phase of PVDF. The conductivity of the solid electrolyte membrane was measured using the AC impedance method to be 2.82×10 -4 S/cm. The tensile strength measured using an electronic universal testing machine is 6MPa, as shown in Figure 3. The lithium sheet/solid electrolyte membrane/steel sheet half-cell linear voltammetry test electrochemical window is 4.5V, and the linear voltammetry curve is shown in Figure 4.
本案例采用扣式电池进行电化学测试,以采用固态电解质浆料B作为粘结剂,正极极片的制备是:将活性物质LFP、固态电解质浆料B、导电碳superP按干重质量百分比94﹕2﹕4进行混合,加入有机溶剂NMP,放入研磨罐进行40分钟研磨,在刮涂机铝箔上涂布成单面厚度60μm正极片,放入烘箱60℃干燥2h,用裁片机裁至直径为12mm的正极极片,负极为直径15mm的锂金属负极,以本实施例制备的固态电解质膜为隔膜,裁至直径19mm固态电解质膜。待正极片在真空烘箱100℃干燥20小时后,在手套箱,将固态电解质膜放置在正电极和负电极之间,并在正极侧,负极侧各加入5μL六氟磷酸锂商用电解液,达到润湿极片的效果,并组装扣式电池,在充放电测试仪上进行0.2C倍率充放电测试,放电比容量为149mAh/g。In this case, a button cell is used for electrochemical testing, and solid electrolyte slurry B is used as the binder. The preparation of the positive electrode sheet is: the active material LFP, solid electrolyte slurry B, and conductive carbon superP are mixed according to the dry weight mass percentage of 94 ﹕2﹕4 Mix, add the organic solvent NMP, put it into a grinding tank and grind it for 40 minutes. Coat it on the aluminum foil of a scraper coater to form a single-sided positive electrode sheet with a thickness of 60 μm. Put it in an oven to dry at 60°C for 2 hours, and cut it with a cutting machine. The positive electrode piece has a diameter of 12 mm, and the negative electrode is a lithium metal negative electrode with a diameter of 15 mm. The solid electrolyte membrane prepared in this embodiment is used as a separator, and the solid electrolyte membrane is cut to a diameter of 19 mm. After the positive electrode sheet is dried in a vacuum oven at 100°C for 20 hours, place the solid electrolyte membrane between the positive electrode and the negative electrode in the glove box, and add 5 μL of lithium hexafluorophosphate commercial electrolyte to the positive and negative electrode sides to wet the electrode. The effect of the chip was tested, and the button battery was assembled, and a 0.2C rate charge and discharge test was performed on the charge and discharge tester. The discharge specific capacity was 149mAh/g.
实施例2-6与实施例1制备方法相同,不同的是预锂化聚苯硫醚、PVDF、锂盐的比例不同。具体实施例2-6的预锂化聚苯硫醚、PVDF、锂盐的比例详见表1。The preparation methods of Examples 2-6 are the same as those of Example 1, except that the proportions of prelithiated polyphenylene sulfide, PVDF, and lithium salt are different. The proportions of prelithiated polyphenylene sulfide, PVDF, and lithium salt in specific embodiments 2-6 are detailed in Table 1.
实施例Example
实施例7与实施例2制备方法相同,不同的是负极采用无负极金属Cu,具体为磷酸、硝酸处理后的铜箔。The preparation method of Example 7 is the same as that of Example 2, except that the negative electrode uses Cu without negative electrode metal, specifically copper foil treated with phosphoric acid and nitric acid.
此对比例与上述实施例制备方法相同,不同的是没有加入预锂化聚苯硫醚粉体的PVDF与锂盐的聚合物电解质。The preparation method of this comparative example is the same as that of the above embodiment, except that the polymer electrolyte of PVDF and lithium salt of prelithiated polyphenylene sulfide powder is not added.
具体实施例1-7及对比例的电化学性能对比情况列于表1。The electrochemical performance comparison of specific examples 1-7 and comparative examples is listed in Table 1.
表1不同实施例聚合物固态电解质成分及电化学性能Table 1 Composition and electrochemical properties of polymer solid electrolytes in different embodiments
尽管已经描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although the embodiments of the present invention have been described, it will be understood by those of ordinary skill in the art that various changes, modifications, substitutions and variations can be made in these embodiments without departing from the principles and spirit of the invention. The scope of the invention is defined by the appended claims and their equivalents.
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CN111342121A (en) * | 2020-02-10 | 2020-06-26 | 江苏大学 | Pre-lithiated polyphenylene sulfide with high solid lithium solubility, and preparation method and application thereof |
CN111864272A (en) * | 2020-06-09 | 2020-10-30 | 江苏大学 | A kind of high safety and high volume energy density quasi-solid-state lithium ion battery and its manufacturing method |
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