CN115132961A - A kind of sodium ion battery positive electrode and its preparation method and application - Google Patents
A kind of sodium ion battery positive electrode and its preparation method and application Download PDFInfo
- Publication number
- CN115132961A CN115132961A CN202210743116.9A CN202210743116A CN115132961A CN 115132961 A CN115132961 A CN 115132961A CN 202210743116 A CN202210743116 A CN 202210743116A CN 115132961 A CN115132961 A CN 115132961A
- Authority
- CN
- China
- Prior art keywords
- sodium
- positive electrode
- polymer
- ion
- ion battery
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- 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
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
-
- 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
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/137—Electrodes based on electro-active polymers
-
- 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
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
-
- 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
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
- H01M4/1399—Processes of manufacture of electrodes based on electro-active polymers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
- H01M4/622—Binders being polymers
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Secondary Cells (AREA)
Abstract
Description
技术领域technical field
本发明属于钠离子电池技术领域,涉及一种钠离子电池正极极片及其制备方法和应用。The invention belongs to the technical field of sodium ion batteries, and relates to a positive pole piece of a sodium ion battery and a preparation method and application thereof.
背景技术Background technique
钠离子电池是一种类似锂离子电池的摇椅式二次电池。相比于锂离子电池,其钠离子第一电离能更低,这使得钠离子更稳定,在低温下不易析出枝晶,为钠离子电池带来更加优异的安全性、稳定性与低温性能。其二,钠离子摩尔电导率更高,钠离子电池电化学性能也略优于锂离子电池。钠资源供需关系稳定,价格波动小。钠离子固态电池是一种电池科技,其采用不可燃的钠离子固态电池电解质替换了可燃性的有机液态电解质,大幅提升了电池系统的安全性,同时能够更好地适配高能量正负极并减轻系统重量,实现能量密度同步提升。A sodium-ion battery is a rocking-chair secondary battery similar to a lithium-ion battery. Compared with lithium-ion batteries, the first ionization energy of sodium ions is lower, which makes sodium ions more stable, and it is not easy to precipitate dendrites at low temperatures, which brings more excellent safety, stability and low-temperature performance to sodium-ion batteries. Second, the molar conductivity of sodium ions is higher, and the electrochemical performance of sodium ion batteries is slightly better than that of lithium ion batteries. The supply and demand relationship of sodium resources is stable, and the price fluctuation is small. The sodium-ion solid-state battery is a battery technology that replaces the flammable organic liquid electrolyte with a non-flammable sodium-ion solid-state battery electrolyte, which greatly improves the safety of the battery system and can better adapt to high-energy positive and negative electrodes. And reduce the weight of the system to achieve a simultaneous increase in energy density.
目前钠离子固态电池中的固态正极极片通常采用匀浆、涂布的工艺制作而成,为了保证电解质膜能够连续,在匀浆步骤中需要将粘结剂、溶剂与固态电解质颗粒进行混合。At present, the solid cathode electrode in sodium-ion solid-state batteries is usually made by homogenization and coating process. In order to ensure the continuity of the electrolyte membrane, it is necessary to mix the binder, the solvent and the solid electrolyte particles in the homogenization step.
CN114023921A公开了一种钠离子电池正极极片及其制备方法和应用,所述钠离子电池正极极片的活性材料包括聚三苯胺和/或聚三苯胺衍生物,其使用聚三苯胺和/或聚三苯胺衍生物作为正极活性材料,聚三苯胺及其衍生物具备聚对苯导电聚合物的快速充放电传输骨架而表现出优异的功率特性,同时兼具聚苯胺的高能量氧化还原基团而具有较高的能量密度。CN114023921A discloses a sodium ion battery positive pole piece and its preparation method and application, the active material of the sodium ion battery positive pole piece includes polytriphenylamine and/or polytriphenylamine derivative, which uses polytriphenylamine and/or Polytriphenylamine derivatives are used as cathode active materials. Polytriphenylamine and its derivatives have the fast charge-discharge transport framework of poly(paraphenylene) conductive polymers and exhibit excellent power characteristics. At the same time, they have high-energy redox groups of polyaniline. and has a higher energy density.
CN110429329A公开了一种全固态钠离子电池的制备方法,包括:将钠盐、有机溶剂、添加剂和引发剂混合,得到液态混合液;在正极极片和/或负极极片的表面上涂覆形成固态电解质层;封装,得到钠离子电芯;将钠离子电芯烘烤后注入液态混合液,静置;加热钠离子电芯,得到未活化的固态钠离子电池;将固态钠离子电池经过化成、除气、真空封装,得到全固态钠离子电池。CN110429329A discloses a preparation method of an all-solid-state sodium ion battery, comprising: mixing sodium salt, organic solvent, additive and initiator to obtain a liquid mixture; coating the surface of the positive pole piece and/or the negative pole piece to form a solid electrolyte layer; encapsulation to obtain a sodium ion battery; after baking the sodium ion battery, inject it into a liquid mixture, and let it stand; heating the sodium ion battery to obtain an unactivated solid state sodium ion battery; converting the solid sodium ion battery into , degassing, and vacuum packaging to obtain an all-solid-state sodium-ion battery.
上述方案所述钠离子电池均采用常规的粘结剂,其使用的粘结剂不具有离子导电性,且当粘结剂溶解于溶剂中再干燥之后,粘结剂会包覆于固态电解质的颗粒表面,导致离子在颗粒之间传输不顺畅,从而使得固体正极极片的离子电导率显著下降,最终造成电池的倍率性能与容量发挥的严重损失。且由于粘结剂会包覆于固态电解质的颗粒表面,从而加大了粘结剂的使用量;此外,溶剂的添加增加了烘干、溶剂回收处理等工序,增加了成本且可能造成环境污染。The sodium-ion batteries described in the above solutions all use conventional binders, the binders used do not have ionic conductivity, and when the binder is dissolved in the solvent and then dried, the binder will be coated on the solid electrolyte. On the surface of the particles, the ions are not transported smoothly between the particles, so that the ionic conductivity of the solid positive electrode sheet is significantly reduced, and eventually the rate performance and capacity of the battery are seriously lost. And because the binder will coat the particle surface of the solid electrolyte, the usage of the binder is increased; in addition, the addition of the solvent increases the drying, solvent recovery and other processes, which increases the cost and may cause environmental pollution. .
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种钠离子电池正极极片及其制备方法和应用,本发明所述正极极片以可纤维化、可传导钠离子的聚合物作为粘结剂,通过细丝状的可纤维化聚合物将固态电解质颗粒连接起来,所述粘结剂在能够在颗粒之间起到传导钠离子的作用,通过该方法所制备的固态正极极片具有比使用非离子导体所制备的固态正极极片具有更低的传输阻抗,因此通过其制备得到的固体电池具有优异的倍率性能。The purpose of the present invention is to provide a kind of positive pole piece of sodium ion battery and its preparation method and application. The fiberizable polymer connects the solid electrolyte particles, and the binder acts to conduct sodium ions between the particles. The solid-state positive electrode sheet has lower transmission impedance, so the solid-state battery prepared by it has excellent rate performance.
为达到此发明目的,本发明采用以下技术方案:In order to achieve this object of the invention, the present invention adopts the following technical solutions:
第一方面,本发明提供了一种钠离子电池正极极片,所述钠离子电池正极极片包括集流体和设置于所述集流体表面的活性物质层,所述活性物质层包括钠离子活性物质、钠离子固态电解质、导电剂和可纤化聚合物,所述可纤化聚合物的主链包含-[CF2-CF2]n-,所述可纤化聚合物的支链包括-SO3 -。In a first aspect, the present invention provides a positive electrode plate for a sodium ion battery, the positive electrode plate for a sodium ion battery includes a current collector and an active material layer disposed on the surface of the current collector, and the active material layer includes a sodium ion active material layer. A substance, a sodium ion solid electrolyte, a conductive agent, and a fiberizable polymer, the main chain of the fiberizable polymer containing -[CF 2 -CF 2 ] n -, and the branched chain of the fiberizable polymer including - SO 3 - .
本发明所述可纤化聚合物一部分为:由-[CF2-CF2]n-构成的主链结构,其提供聚合物的粘结力与可纤维化特性,另一部分为由具有Na+离子交换功能基团-SO3H构成的支链,该支链通过Na+离子交换后形成-SO3Na,起到传导钠离子的作用。Part of the fiberizable polymer of the present invention is: the main chain structure composed of -[CF 2 -CF 2 ] n -, which provides the cohesive force and fiberizable properties of the polymer, and the other part is composed of Na + The branch chain formed by the ion exchange functional group -SO 3 H, the branch chain forms -SO 3 Na after Na + ion exchange, and plays the role of conducting sodium ions.
本发明以可纤维化、可传导钠离子的聚合物作为粘结剂,所述聚合物可连接于部分正极活性层之中的颗粒之间,也可以连接于全部正极活性层之中的颗粒之间,通过细丝状的可纤维化聚合物将固态电解质颗粒连接起来,可纤维化聚合物与固态电解质颗粒之间为点对点接触,能够有效降低固态电解质颗粒之间的离子传输阻抗,降低正极极片颗粒之间的离子传输阻抗以及提高机械性能。通过其制备得到的固体电池具有优异的倍率性能,同时大幅降低了粘结剂用量。In the present invention, a polymer that can be fibrillated and can conduct sodium ions is used as a binder, and the polymer can be connected between the particles in part of the positive electrode active layer, or between the particles in all the positive electrode active layers. The solid electrolyte particles are connected by the filament-like fiberizable polymer, and the point-to-point contact between the fiberizable polymer and the solid electrolyte particles can effectively reduce the ion transfer impedance between the solid electrolyte particles and reduce the positive electrode. Ion transfer resistance between flake particles and improved mechanical properties. The solid battery prepared by this method has excellent rate performance and greatly reduces the amount of binder.
本发明以具有离子导电作用的聚合物作为粘结剂,在起到粘合颗粒的同时,在能够在颗粒之间起到传导钠离子的作用,通过该方法所制备的固态正极极片具有比使用非离子导体所制备的固态正极极片具有更低的传输阻抗,因此通过其制备得到的固体电池具有优异的倍率性能。In the present invention, a polymer with ionic conductivity is used as a binder, which can play a role of conducting sodium ions between the particles while binding the particles. The solid-state positive electrode plate prepared by using the non-ionic conductor has lower transmission impedance, so the solid-state battery prepared by using the non-ionic conductor has excellent rate performance.
优选地,所述可纤化聚合物的电导率>5×10-6S/cm,例如:5.2×10-6S/cm、6×10- 6S/cm、7×10-6S/cm、8×10-6S/cm、9×10-6S/cm或10×10-6S/cm等。Preferably, the electrical conductivity of the fiberizable polymer is >5×10 -6 S/cm, for example: 5.2×10 -6 S/cm , 6×10 -6 S/cm, 7×10 -6 S/cm cm, 8×10 -6 S/cm, 9×10 -6 S/cm or 10×10 -6 S/cm, etc.
优选地,所述可纤维化聚合物呈细丝状。Preferably, the fiberizable polymer is in the form of filaments.
本发明采用细丝状的聚合物作为粘结剂,没有溶剂的参与,一方面避免了溶剂对固态电解质的接触和反应,使电池的阻抗降低,提升电池的倍率性能;另一方面减少了溶剂蒸发、回收所需的能量,避免有机溶剂后处理及回收等问题,有效节约生产成本,避免环境污染;同时该制备过程简单,易于放大,是一种适合于工业应用的方法,有利于推进新能源产业的发展,具有广阔的应用前景。The invention uses filamentous polymer as the binder without the participation of the solvent. On the one hand, the contact and reaction of the solvent to the solid electrolyte is avoided, the impedance of the battery is reduced, and the rate performance of the battery is improved; on the other hand, the solvent is reduced. The energy required for evaporation and recovery avoids problems such as post-processing and recovery of organic solvents, effectively saving production costs and avoiding environmental pollution; at the same time, the preparation process is simple and easy to scale up, which is a method suitable for industrial applications and is conducive to promoting new technologies. The development of the energy industry has broad application prospects.
优选地,所述可纤化聚合物与固态电解质颗粒之间为点对点接触。Preferably, there is point-to-point contact between the fiberizable polymer and the solid electrolyte particles.
优选地,所述正极极片的厚度为30~200μm,例如:30μm、50μm、80μm、100μm、150μm或200μm等。Preferably, the thickness of the positive pole piece is 30-200 μm, for example: 30 μm, 50 μm, 80 μm, 100 μm, 150 μm or 200 μm, etc.
优选地,所述集流体的厚度<20μm。Preferably, the thickness of the current collector is <20 μm.
优选地,所述钠离子活性物质包括层状氧化物材料、聚阴离子型正极材料或普鲁士蓝正极材料中的任意一种或至少两种的组合。Preferably, the sodium ion active material includes any one or a combination of at least two of a layered oxide material, a polyanionic positive electrode material or a Prussian blue positive electrode material.
优选地,所述层状氧化物材料的化学式为NaxMO2,其中,x≤1,M为Ni、Mn、Fe、Co或Cu中的任意一种或至少两种的组合。Preferably, the chemical formula of the layered oxide material is Na x MO 2 , wherein x≤1, and M is any one or a combination of at least two of Ni, Mn, Fe, Co or Cu.
优选地,所述聚阴离子型正极材料的化学式为NaxMy(AO4)z(P2O7)w,其中,2≤x≤4,1≤y≤4,0≤z≤4,0≤w≤1,M包括Ti、V、Cr、Mn、Fe、Co、Ni、Cu或Zn中的任意一种或至少两种的组合,A包括Al、Si、P、S、Ti、V或W中的任意一种或至少两种的组合,M为电活性过渡金属。Preferably, the chemical formula of the polyanionic positive electrode material is Na x My (AO 4 ) z (P 2 O 7 ) w , wherein 2≤x≤4, 1≤y≤4, 0≤z≤4, 0≤w≤1, M includes any one or a combination of at least two of Ti, V, Cr, Mn, Fe, Co, Ni, Cu or Zn, A includes Al, Si, P, S, Ti, V Or any one of W or a combination of at least two of them, and M is an electroactive transition metal.
优选地,所述普鲁士蓝正极材料的化学式为AxM[Fe(CN)6]y·zH2O,其中,0<x<2,0<y<1,A包括Li、Na或K中的任意一种或至少两种的组合,M包括Fe、Mn、Co、Ni或Cu中的任意一种或至少两种的组合。Preferably, the chemical formula of the Prussian blue cathode material is A x M[Fe(CN) 6 ] y ·zH 2 O, wherein 0<x<2, 0<y<1, and A includes Li, Na or K Any one or a combination of at least two of M includes any one or a combination of at least two of Fe, Mn, Co, Ni or Cu.
优选地,所述钠离子固态电解质包括Na-β-Al2O3、Na3PS4、Na3SbS4或Na11Sn2PS12中的任意一种或至少两种的组合。Preferably, the sodium ion solid electrolyte comprises any one or a combination of at least two of Na-β-Al 2 O 3 , Na 3 PS 4 , Na 3 SbS 4 or Na 11 Sn 2 PS 12 .
优选地,所述导电剂包括乙炔黑、Super-P、碳纳米管、碳纤维(VGCF)、科琴黑、石墨导电剂或石墨烯中的任意一种或至少两种的组合。Preferably, the conductive agent comprises any one or a combination of at least two of acetylene black, Super-P, carbon nanotube, carbon fiber (VGCF), Ketjen black, graphite conductive agent or graphene.
优选地,以所述活性物质层的质量为100%计,所述钠离子活性物质的质量分数为55~90%,例如:55%、60%、70%、80%或90%等,优选为70~85%。Preferably, based on the mass of the active material layer as 100%, the mass fraction of the sodium ion active material is 55-90%, for example: 55%, 60%, 70%, 80% or 90%, etc., preferably 70 to 85%.
优选地,所述导电剂的质量分数为0.1~5%,例如:0.1%、0.5%、1%、3%或5%等,优选为1~2.5%。Preferably, the mass fraction of the conductive agent is 0.1-5%, for example: 0.1%, 0.5%, 1%, 3% or 5%, etc., preferably 1-2.5%.
优选地,所述可纤化聚合物的质量分数为0.1~5%,例如:0.1%、0.5%、1%、3%或5%等,优选为0.5~3%。Preferably, the mass fraction of the fiberizable polymer is 0.1-5%, for example: 0.1%, 0.5%, 1%, 3% or 5%, etc., preferably 0.5-3%.
第二方面,本发明提供了一种如第一方面所述钠离子电池正极极片的制备方法,所述制备方法包括以下步骤:In a second aspect, the present invention provides a method for preparing a sodium-ion battery positive electrode plate as described in the first aspect, the preparation method comprising the following steps:
(1)对可纤化聚合物进行钠离子交换处理,将钠离子正极活性物质、固态电解质颗粒、导电剂和可纤化聚合物搅拌混合,得到混合料;(1) performing sodium ion exchange treatment on the fiberizable polymer, stirring and mixing the sodium ion positive electrode active material, solid electrolyte particles, conductive agent and fiberizable polymer to obtain a mixture;
(2)对步骤(1)得到的混合料进行剪切和热压处理得到正极活性物质层;(2) shearing and hot pressing the mixture obtained in step (1) to obtain a positive electrode active material layer;
(3)将步骤(2)得到的正极活性物质层压覆在集流体表面得到所述钠离子电池正极极片。(3) Coating the positive electrode active material layer obtained in step (2) on the surface of the current collector to obtain the sodium ion battery positive electrode sheet.
本发明采用可纤维化聚合物作为粘结剂,在不添加溶剂的情况下,首先将钠离子活性物质、钠离子固态电解质、导电剂混合;其次将可纤维化聚合物和上述混合颗粒在低速下混合均匀,混合后再进行高速剪切混合,利用可纤维化聚合物在外部剪切力的作用下能够丝状化的特点,将可纤维化聚合物拉长、拉细,及丝状化,丝状化的可纤维化聚合物具有黏粘性,能够将各颗粒粘合在一起;且由于可纤维化聚合物丝状化后呈细丝状存在,其于固态电解质颗粒之间为点-点接触,区别于传统湿法涂布过程中粘结剂与颗粒之间的面-面接触,本发明所述方法能够降低固态电解质颗粒之间的离子传输阻抗,提高机械性能,通过其制备得到的固体电池具有优异的倍率性能,同时相比于传统的湿法涂布工艺能够降低粘结剂的使用量。In the present invention, the fiberizable polymer is used as the binder, and without adding a solvent, the sodium ion active material, the sodium ion solid electrolyte and the conductive agent are first mixed; secondly, the fiberizable polymer and the above mixed particles are mixed at a low speed Mix evenly, and then carry out high-speed shear mixing. The fiberizable polymer can be elongated, thinned, and filamentized by using the characteristics that the fiberizable polymer can be filamentous under the action of external shearing force. , the filamentous fiberizable polymer is sticky and can bind the particles together; and since the fiberizable polymer exists in the form of filaments after filamentation, it is a point between the solid electrolyte particles- Point contact, which is different from the surface-to-surface contact between the binder and the particles in the traditional wet coating process, the method of the present invention can reduce the ion transmission resistance between the solid electrolyte particles and improve the mechanical properties. The solid-state battery has excellent rate performance and can reduce the amount of binder used compared to the traditional wet coating process.
本发明对混合料进行剪切进行热压处理,从而达到将固态正极极片薄膜化、厚度均一化的目的,热压后能够形成自支撑的独立正极极片,最后再将该正极极片与集流体热压复合。该工艺制备的正极极片延展性好,可塑性强,经过反复辊压能够达到较高的压实密度,能有效提升电池的体积能量密度和质量能量密度,且对于正极极片的形状与尺寸均无要求,能够根据实际要求而改变与定制,具有更高的灵活性。In the present invention, the mixture is sheared and hot-pressed, so as to achieve the purpose of thinning the solid positive electrode piece and making the thickness uniform. After hot-pressing, a self-supporting independent positive electrode piece can be formed. The collector is hot-pressed composite. The positive electrode piece prepared by this process has good ductility and strong plasticity. After repeated rolling, it can achieve a high compaction density, which can effectively improve the volume energy density and mass energy density of the battery. No requirements, can be changed and customized according to actual requirements, with higher flexibility.
优选地,所述钠离子交换处理的方式包括以下步骤:Preferably, the mode of the sodium ion exchange treatment comprises the following steps:
(A)将可纤化聚合物和盐酸溶液混合浸泡后洗涤至中性;(A) mixing and soaking the fiberizable polymer and hydrochloric acid solution and washing to neutrality;
(B)将步骤(1)得到的聚合物干燥后过筛,与氯化钠溶液混合,经洗涤干燥处理得到含钠离子的可纤化聚合物。(B) the polymer obtained in step (1) is dried, sieved, mixed with sodium chloride solution, washed and dried to obtain a sodium ion-containing fiberizable polymer.
以PTFE为例,其离子交换步骤如下所示:Taking PTFE as an example, its ion exchange steps are as follows:
对上述所制备的聚合物使用FTIR进行表征,可以看出,其在1130cm-1、1200cm-1附近处存在-[CF2-CF2]n-链段基团的吸收峰,且在1060cm-1处存在-SO3 -基团的吸收峰。Using FTIR to characterize the polymer prepared above, it can be seen that there are absorption peaks of -[CF 2 -CF 2 ] n -segment groups around 1130cm -1 and 1200cm -1 , and at 1060cm - There is an absorption peak of -SO 3 - group at 1 .
优选地,所述高速混合的速度为500~3000rpm,例如:500rpm、1000rpm、2000rpm、2500rpm或3000rpm等。Preferably, the speed of the high-speed mixing is 500-3000 rpm, for example: 500 rpm, 1000 rpm, 2000 rpm, 2500 rpm or 3000 rpm and the like.
本发明中,若转速过低、时间过短,则外加机械力不足以拉伸粘结剂使其丝状化,从而不能使粘结剂达到最佳的粘结状态;若转速过高、时间过长,则过大的外加机械力会使得粘结剂过度拉伸、延长而产生断裂,使得粘结剂形成片段化的短小细丝,这最终也会造成粘结力的下降。In the present invention, if the rotational speed is too low and the time is too short, the external mechanical force is not enough to stretch the adhesive to make it filamentous, so that the adhesive cannot reach the optimal bonding state; if the rotational speed is too high, the time If it is too long, the excessively large external mechanical force will cause the adhesive to be overstretched, elongated and fractured, so that the adhesive will form fragmented short filaments, which will eventually lead to a decrease in the adhesive force.
优选地,所述高速混合的时间为10~60min,例如:10min、20min、30min、40min、50min或60min等。Preferably, the high-speed mixing time is 10-60 minutes, for example: 10 minutes, 20 minutes, 30 minutes, 40 minutes, 50 minutes, or 60 minutes.
优选地,所述热压处理的温度为50~220℃,例如:50℃、80℃、100℃、200℃或220℃等。Preferably, the temperature of the hot pressing treatment is 50-220°C, for example: 50°C, 80°C, 100°C, 200°C or 220°C, and the like.
第三方面,本发明提供了一种钠离子固态电池,所述钠离子固态电池包含如第一方面所述的钠离子电池正极极片。In a third aspect, the present invention provides a sodium-ion solid-state battery, the sodium-ion solid-state battery comprising the sodium-ion battery positive electrode plate described in the first aspect.
相对于现有技术,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明所述正极极片以可纤维化、可传导钠离子的聚合物作为粘结剂。相比于传统的湿法涂布工艺,不需溶剂的参与;且通过细丝状的可纤维化聚合物将固态电解质颗粒连接起来,可纤维化聚合物与固态电解质颗粒之间为点对点接触,能够有效降低固态电解质颗粒之间的离子传输阻抗,降低正极极片颗粒之间的离子传输阻抗以及提高机械性能。通过其制备得到的固体电池具有优异的倍率性能,同时大幅降低了粘结剂用量。(1) The positive electrode sheet of the present invention uses a polymer that can be fiberized and can conduct sodium ions as a binder. Compared with the traditional wet coating process, no solvent is required; and the solid electrolyte particles are connected by filament-like fiberizable polymers, and the fiberizable polymer and the solid electrolyte particles are in point-to-point contact. The ion transport resistance between solid electrolyte particles can be effectively reduced, the ion transport resistance between positive electrode and pole piece particles can be reduced, and the mechanical properties can be improved. The solid battery prepared by this method has excellent rate performance and greatly reduces the amount of binder.
(2)本发明以具有离子导电作用的聚合物作为粘结剂,在起到粘合颗粒的同时,在能够在颗粒之间起到传导钠离子的作用,通过该方法所制备的固态正极极片具有比使用非离子导体所制备的固态正极极片具有更低的传输阻抗,因此通过其制备得到的固体电池具有优异的倍率性能。(2) The present invention uses a polymer with ionic conductivity as a binder, which can play a role of conducting sodium ions between the particles while binding the particles. The solid positive electrode prepared by this method The sheet has lower transmission impedance than the solid-state positive electrode sheet prepared by using the non-ionic conductor, so the solid-state battery prepared therefrom has excellent rate performance.
(3)本发明所述钠离子电池正极极片的拉伸强度可达115.2N/cm2以上,0.33C放电比容量可达93.8mAh/g以上,1C放电比容量可达90mAh/g以上,3C放电比容量可达97.2mAh/g以上,1C/0.1C保持率可达91.3%以上,3C/0.1C保持率可达87.6%以上。(3) The tensile strength of the positive electrode piece of the sodium ion battery according to the present invention can reach more than 115.2N/cm 2 , the specific capacity of 0.33C discharge can reach more than 93.8mAh/g, and the specific capacity of 1C discharge can reach more than 90mAh/g, The 3C discharge specific capacity can reach more than 97.2mAh/g, the 1C/0.1C retention rate can reach more than 91.3%, and the 3C/0.1C retention rate can reach more than 87.6%.
附图说明Description of drawings
图1是实施例1所述钠离子电池正极极片的SEM图。FIG. 1 is a SEM image of the positive electrode piece of the sodium-ion battery described in Example 1. FIG.
图2是钠离子交换后的可纤维化聚合物的FTIR图谱。Figure 2 is an FTIR spectrum of the fiberizable polymer after sodium ion exchange.
具体实施方式Detailed ways
下面通过具体实施方式来进一步说明本发明的技术方案。本领域技术人员应该明了,所述实施例仅仅是帮助理解本发明,不应视为对本发明的具体限制。The technical solutions of the present invention are further described below through specific embodiments. It should be understood by those skilled in the art that the embodiments are only for helping the understanding of the present invention, and should not be regarded as a specific limitation of the present invention.
本发明实施例和对比例使用的可纤化聚合物的钠离子交换过程如下:The sodium ion exchange process of the fibrillable polymers used in the examples of the present invention and the comparative examples is as follows:
1)首先将10g上述聚合物使用100ml、5mol/L的HCl溶液浸泡32h;1) First, soak 10g of the above-mentioned polymer in 100ml, 5mol/L of HCl solution for 32h;
2)浸泡后使用过量去离子水将上述聚合物清洗,直至PH值为中性;2) Use excess deionized water to clean the above-mentioned polymer after soaking until the pH value is neutral;
3)将步骤2中所得聚合物在120℃下干燥8h;3) drying the polymer obtained in step 2 at 120°C for 8h;
4)将步骤3中聚合物颗粒使用300目超声振动筛进行筛分处理,取筛网下层的物料备用;4) use 300-mesh ultrasonic vibrating screen to carry out sieving treatment of polymer particles in step 3, and take the material in the lower layer of the screen for subsequent use;
5)将NaCl溶解于去离子水之中,质量浓度为30%;5) NaCl is dissolved in deionized water, and the mass concentration is 30%;
6)将步骤4中所得聚合物颗粒2g与步骤5之中的溶液50ml混合,在60℃下以1200rpm转速搅拌30h;6) Mix 2 g of polymer particles obtained in step 4 with 50 ml of the solution in step 5, and stir at 1200 rpm for 30 h at 60°C;
7)将步骤6中所得聚合物使用去离子水清洗至表面无NaCl残留;7) using deionized water to clean the obtained polymer in step 6 to the surface without NaCl residue;
8)将步骤7所得聚合物在120℃下干燥8h备用,制得聚合物的FTIR图谱如图2所示。8) The polymer obtained in step 7 was dried at 120° C. for 8 h for use, and the FTIR spectrum of the obtained polymer was shown in FIG. 2 .
实施例1Example 1
本实施例提供了一种钠离子电池正极极片,所述钠离子电池正极极片的制备方法如下:The present embodiment provides a sodium ion battery positive pole piece, and the preparation method of the sodium ion battery positive pole piece is as follows:
(1)将Na3V2(PO4)3、Na3PS4和Super-P放入搅拌机中,上述各物质比例为75:23:2,以350rpm搅拌速度搅拌60min,得到混合物,将所述混合物与钠离子交换后的可纤化聚合物共同加入搅拌机中进行低速搅拌混合,聚合物与混合物料的比例为2:98,所述搅拌转速为300rpm,搅拌时间为20min,得到混合料;(1) Put Na 3 V 2 (PO 4 ) 3 , Na 3 PS 4 and Super-P into a mixer, the ratio of each of the above-mentioned substances is 75:23:2, and stir for 60min at a stirring speed of 350rpm to obtain a mixture. The mixture and the fibrillable polymer after the sodium ion exchange are added together in the mixer for low-speed stirring and mixing, the ratio of the polymer and the mixture is 2:98, the stirring speed is 300rpm, and the stirring time is 20min to obtain the mixture;
(2)将上述混合料使用高速混合机进行剪切混合,得到剪切混合料,所述高速搅拌的转速为2500rpm,搅拌时间为40min,将剪切混合料放入辊压机中进行热压处理使之形成自支撑正极活性物质层,其中所述热压温度为60℃,辊压速度为50cm/min,正极活性物质层的厚度为60μm;(2) the above-mentioned mixture is sheared and mixed using a high-speed mixer to obtain a sheared mixture, the rotating speed of the high-speed stirring is 2500rpm, and the stirring time is 40min, and the sheared mixture is put into the roller press and hot-pressed processing to form a self-supporting positive electrode active material layer, wherein the hot pressing temperature is 60° C., the rolling speed is 50 cm/min, and the thickness of the positive electrode active material layer is 60 μm;
(3)将正极活性物质层与铝箔热压在一起,得到所述钠离子电池正极极片。(3) Hot pressing the positive electrode active material layer and the aluminum foil together to obtain the positive electrode piece of the sodium ion battery.
所述正极极片的SEM图如图1所示,其中的颗粒为固态电解质颗粒,细丝状的为丝状化后的聚合物,圆圈处可以看出细丝状的聚合物与固态电解质颗粒之间为点对点接触。The SEM image of the positive electrode plate is shown in Figure 1, the particles are solid electrolyte particles, the filamentous polymer is filamentous, and the filamentous polymer and solid electrolyte particles can be seen in the circle. point-to-point contact.
实施例2Example 2
本实施例提供了一种钠离子电池正极极片,所述钠离子电池正极极片的制备方法如下:The present embodiment provides a sodium ion battery positive pole piece, and the preparation method of the sodium ion battery positive pole piece is as follows:
(1)将Na3V2(PO4)3、Na3SbS4和VGCF放入搅拌机中,上述各物质比例为80:19:1,以400rpm搅拌速度搅拌80min,得到混合物,将所述混合物与钠离子交换后的可纤化聚合物共同加入搅拌机中进行低速搅拌混合,聚合物与混合物料的比例为1:99,所述搅拌转速为400rpm,搅拌时间为20min,得到混合料;(1) Put Na 3 V 2 (PO 4 ) 3 , Na 3 SbS 4 and VGCF into a mixer, the ratio of each of the above substances is 80:19:1, and stir for 80 min at a stirring speed of 400 rpm to obtain a mixture. Add the fibrillable polymer after the sodium ion exchange into the mixer for low-speed stirring and mixing, the ratio of the polymer to the mixture is 1:99, the stirring speed is 400rpm, and the stirring time is 20min to obtain the mixture;
(2)将上述混合料使用高速混合机进行剪切混合,得到剪切混合料,所述高速搅拌的转速为3000rpm,搅拌时间为40min,将剪切混合料放入辊压机中进行热压处理使之形成自支撑正极活性物质层,其中所述热压温度为80℃,辊压速度为60cm/min,正极活性物质层的厚度为60μm;(2) the above-mentioned mixed material is sheared and mixed using a high-speed mixer to obtain a sheared mixed material, the rotating speed of the described high-speed stirring is 3000rpm, and the stirring time is 40min, and the sheared mixed material is put into the roller press and hot-pressed processing to form a self-supporting positive electrode active material layer, wherein the hot pressing temperature is 80° C., the rolling speed is 60 cm/min, and the thickness of the positive electrode active material layer is 60 μm;
(3)将正极活性物质层与铝箔热压在一起,得到所述钠离子电池正极极片。(3) Hot pressing the positive electrode active material layer and the aluminum foil together to obtain the positive electrode piece of the sodium ion battery.
实施例3Example 3
本实施例与实施例1区别仅在于,所述聚合物与混合物料的比例为0.5:99.5,其他条件与参数与实施例1完全相同。The only difference between this example and Example 1 is that the ratio of the polymer to the mixed material is 0.5:99.5, and other conditions and parameters are exactly the same as those of Example 1.
实施例4Example 4
本实施例与实施例1区别仅在于,所述聚合物与混合物料的比例为3.5:96.5,其他条件与参数与实施例1完全相同。The only difference between this example and Example 1 is that the ratio of the polymer to the mixed material is 3.5:96.5, and other conditions and parameters are exactly the same as those of Example 1.
对比例1Comparative Example 1
本对比例提供一种钠离子正极极片的制备方法,包括如下步骤:The present comparative example provides a method for preparing a sodium ion positive pole piece, comprising the following steps:
(1)将Na3V2(PO4)3、Na3PS4和SP放入搅拌机中,上述各物质比例为75:23:2,以350rpm搅拌速度搅拌60min,得到混合物;(1) put Na 3 V 2 (PO 4 ) 3 , Na 3 PS 4 and SP into the mixer, the above-mentioned respective material ratios are 75:23:2, and stir 60min at a stirring speed of 350rpm to obtain a mixture;
(2)占整个粉体质量2%的丁腈橡胶与甲苯溶剂进行溶解;(2) the nitrile rubber and toluene solvent accounting for 2% of the mass of the whole powder are dissolved;
(3)将步骤(2)中溶解的浆料与步骤(1)中将混合好的浆料使用匀浆机进行匀浆;(3) using a homogenizer to homogenize the slurry dissolved in the step (2) and the mixed slurry in the step (1);
(4)最后将上述浆料使用涂布机进行涂布,涂布速度1m/min,涂布后在90℃下干燥2h后,制成正极极片,正极极片的厚度为60μm。(4) Finally, the above slurry is coated with a coating machine at a coating speed of 1 m/min. After coating, it is dried at 90° C. for 2 hours to form a positive pole piece, and the thickness of the positive pole piece is 60 μm.
对比例2Comparative Example 2
本对比例提供一种钠离子全固态电池正极极片的制备方法,包括如下步骤:This comparative example provides a preparation method of a sodium ion all-solid-state battery positive pole piece, comprising the following steps:
(1)将Na3V2(PO4)3、Na3SbS4和VGCF放入搅拌机中,上述各物质比例为80:19:1,以400rpm搅拌速度搅拌80min,得到混合物;(1) put Na 3 V 2 (PO 4 ) 3 , Na 3 SbS 4 and VGCF into the mixer, the above-mentioned respective material ratios are 80:19:1, and stirred for 80min at a stirring speed of 400rpm to obtain a mixture;
(2)占整个粉体质量5%的丁腈橡胶与甲苯溶剂进行溶解;(2) the nitrile rubber and toluene solvent accounting for 5% of the mass of the whole powder are dissolved;
(3)将步骤(2)中溶解的浆料与步骤(1)中将混合好的浆料使用匀浆机进行匀浆;(3) using a homogenizer to homogenize the slurry dissolved in the step (2) and the mixed slurry in the step (1);
(4)最后将上述浆料使用涂布机进行涂布,涂布速度1m/min,涂布后在90℃下干燥2h后,制成正极极片,正极极片的厚度为60μm。(4) Finally, the above slurry is coated with a coating machine at a coating speed of 1 m/min. After coating, it is dried at 90° C. for 2 hours to form a positive pole piece, and the thickness of the positive pole piece is 60 μm.
对比例3Comparative Example 3
本对比例与实施例1区别仅在于,不对聚合物进行钠离子交换处理,其他条件与参数与实施例1完全相同。The only difference between this comparative example and Example 1 is that the polymer is not subjected to sodium ion exchange treatment, and other conditions and parameters are exactly the same as those of Example 1.
性能测试:Performance Testing:
对实施例1和对比例1中各材料的电导率进行测试,测试结果如表1所示:The electrical conductivity of each material in Example 1 and Comparative Example 1 is tested, and the test results are shown in Table 1:
表1Table 1
由表1可以看出,由于使用本发明中具有钠离子导电性的聚合物作为粘结剂,“序号2”样品相比于“序号3”样品具有更高的钠离子电导率,也更接近“序号1”原始样品的电导率,即颗粒之间的钠离子传导阻抗更小。而“序号2”、“序号3”样品由于使用具有纤维化能力的粘结剂从而相比于“序号4”样品具有更高的电导率。As can be seen from Table 1, due to the use of the polymer with sodium ion conductivity in the present invention as a binder, the "No. 2" sample has a higher sodium ion conductivity than the "No. 3" sample, which is also closer to The conductivity of the "No. 1" original sample, ie the sodium ion conduction impedance between the particles, is smaller. The "No. 2" and "No. 3" samples have higher electrical conductivity than the "No. 4" samples due to the use of a binder with fibrillation ability.
对实施例1-4和对比例1-3制得正极极片进行拉伸强度测试,将上述制备的正极极片使用切片机裁切为直径为10mm的圆片备用,将200mg钠离子固态电解质Na3PS4放置于直径为10mm的模具套筒中,施加200MPa的压力,使其成为片状,.使用金属Na作为负极,将正极极片、钠片分别放置于步骤2中制备的固态电解质片的两侧,并在外施加50MPa的压力后成型,将上述电池在0.33C、1C、3C的倍率下进行充放电测试,测试结果如表1所示:The positive pole pieces prepared in Examples 1-4 and Comparative Examples 1-3 were tested for tensile strength, and the positive pole pieces prepared above were cut into circular pieces with a diameter of 10 mm using a slicer, and 200 mg of sodium ion solid electrolyte was used. Na 3 PS 4 is placed in a mold sleeve with a diameter of 10 mm, and a pressure of 200 MPa is applied to make it into a sheet. Using metal Na as the negative electrode, the positive electrode and sodium sheet are respectively placed in the solid electrolyte prepared in step 2. The two sides of the sheet were formed, and the pressure of 50MPa was applied outside. The above-mentioned batteries were charged and discharged at the rate of 0.33C, 1C, and 3C. The test results are shown in Table 1:
表1Table 1
由表1可以看出,由实施例1-2可得,本发明所述钠离子电池正极极片的拉伸强度可达115.2N/cm2以上,0.33C放电比容量可达102.8mAh/g以上,1C放电比容量可达93.8mAh/g以上,3C放电比容量可达90mAh/g以上,1C/0.1C保持率可达91.3%以上,3C/0.1C保持率可达87.6%以上。As can be seen from Table 1, from Examples 1-2, the tensile strength of the positive electrode piece of the sodium ion battery of the present invention can reach more than 115.2N/cm 2 , and the discharge specific capacity at 0.33C can reach 102.8mAh/g Above, the 1C discharge specific capacity can reach more than 93.8mAh/g, the 3C discharge specific capacity can reach more than 90mAh/g, the 1C/0.1C retention rate can reach more than 91.3%, and the 3C/0.1C retention rate can reach more than 87.6%.
由实施例1和实施例3-4对比可得,本发明所述钠离子电池正极极片中可纤维化聚合物的添加量会影响制得正极极片的性能,将可纤维化聚合物的添加量控制在0.5~3%,制得正极极片性能较好。若可纤维化聚合物的添加量过大,由于其离子电导率较低过多的添加仍会阻碍离子传输,进而造成倍率性能的下降;若可纤维化聚合物的添加量过小,则粘结力不足,导致极片机型性能差、不能成膜,且造成颗粒间接触不紧密、使得电性能有所降低。From the comparison between Example 1 and Examples 3-4, it can be seen that the addition amount of the fiberizable polymer in the positive electrode plate of the sodium ion battery of the present invention will affect the performance of the obtained positive electrode plate, and the fiberizable polymer The addition amount is controlled at 0.5-3%, and the performance of the prepared positive electrode sheet is good. If the addition amount of the fiberizable polymer is too large, due to its low ionic conductivity, too much addition will still hinder the ion transmission, thereby causing the rate performance to decline; if the addition amount of the fiberizable polymer is too small, the viscosity will Insufficient junction force results in poor performance of the pole piece model, inability to form a film, and the contact between particles is not tight, resulting in a decrease in electrical properties.
由实施例1和对比例1及实施例2和对比例2对比可得,本发明通过细丝状的可纤维化聚合物将固态电解质颗粒连接起来,可纤维化聚合物与固态电解质颗粒之间为点对点接触,能够有效降低固态电解质颗粒之间的离子传输阻抗,降低正极极片颗粒之间的离子传输阻抗以及提高机械性能。以具有离子导电作用的聚合物作为粘结剂,在起到粘合颗粒的同时,在能够在颗粒之间起到传导钠离子的作用,通过该方法所制备的固态正极极片具有比使用非离子导体所制备的固态正极极片具有更低的传输阻抗,因此通过其制备得到的固体电池具有优异的倍率性能。It can be seen from the comparison between Example 1 and Comparative Example 1 and Example 2 and Comparative Example 2 that the present invention connects the solid electrolyte particles through filament-like fiberizable polymers, and the fiberizable polymer and the solid electrolyte particles are connected between the particles. For point-to-point contact, the ion transfer impedance between solid electrolyte particles can be effectively reduced, the ion transfer impedance between positive electrode and pole piece particles can be reduced, and mechanical properties can be improved. Using a polymer with ionic conductivity as a binder, it can play a role of conducting sodium ions between the particles while binding the particles. The solid-state positive electrode plate prepared by the ion conductor has lower transmission impedance, so the solid-state battery prepared by it has excellent rate performance.
由实施例1和对比例3对比可得,本发明对可纤维化聚合物进行钠离子交换处理,可以使聚合物具有一定的钠离子传输能力,进而降低聚合物对离子传输的阻碍作用,从而提升极片的容量发挥与倍率性能。From the comparison between Example 1 and Comparative Example 3, it can be seen that the present invention performs sodium ion exchange treatment on the fiberizable polymer, which can make the polymer have a certain sodium ion transport capacity, thereby reducing the hindering effect of the polymer on ion transport, thereby Improve the capacity and rate performance of the pole piece.
申请人声明,以上所述仅为本发明的具体实施方式,但本发明的保护范围并不局限于此,所属技术领域的技术人员应该明了,任何属于本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,均落在本发明的保护范围和公开范围之内。The applicant declares that the above are only specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto. Those skilled in the art should Changes or substitutions that can be easily conceived within the technical scope all fall within the protection scope and disclosure scope of the present invention.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210743116.9A CN115132961A (en) | 2022-06-27 | 2022-06-27 | A kind of sodium ion battery positive electrode and its preparation method and application |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210743116.9A CN115132961A (en) | 2022-06-27 | 2022-06-27 | A kind of sodium ion battery positive electrode and its preparation method and application |
Publications (1)
Publication Number | Publication Date |
---|---|
CN115132961A true CN115132961A (en) | 2022-09-30 |
Family
ID=83379927
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210743116.9A Pending CN115132961A (en) | 2022-06-27 | 2022-06-27 | A kind of sodium ion battery positive electrode and its preparation method and application |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115132961A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115395090A (en) * | 2022-10-10 | 2022-11-25 | 蜂巢能源科技(无锡)有限公司 | Solid electrolyte membrane and preparation method and application thereof |
CN116314598A (en) * | 2023-05-26 | 2023-06-23 | 江苏正力新能电池技术有限公司 | Dry electrode slice and preparation method and application thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016210419A1 (en) * | 2015-06-26 | 2016-12-29 | Florida State University Research Foundation, Inc. | Dry process method for producing electrodes for electrochemical devices and electrodes for electrochemical devices |
CN108285541A (en) * | 2017-12-29 | 2018-07-17 | 山东东岳高分子材料有限公司 | The exchange membrane containing fluorine and preparation method thereof of nanofiber enhancing |
CN111094438A (en) * | 2017-09-14 | 2020-05-01 | 3M创新有限公司 | Fluorinated copolymers having pendent sulfonyl groups and compositions and articles comprising the same |
CN114388740A (en) * | 2022-01-13 | 2022-04-22 | 江西安驰新能源科技有限公司 | Composite positive electrode for all-solid-state lithium ion battery and preparation method of pole piece of composite positive electrode |
-
2022
- 2022-06-27 CN CN202210743116.9A patent/CN115132961A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016210419A1 (en) * | 2015-06-26 | 2016-12-29 | Florida State University Research Foundation, Inc. | Dry process method for producing electrodes for electrochemical devices and electrodes for electrochemical devices |
CN111094438A (en) * | 2017-09-14 | 2020-05-01 | 3M创新有限公司 | Fluorinated copolymers having pendent sulfonyl groups and compositions and articles comprising the same |
CN108285541A (en) * | 2017-12-29 | 2018-07-17 | 山东东岳高分子材料有限公司 | The exchange membrane containing fluorine and preparation method thereof of nanofiber enhancing |
CN114388740A (en) * | 2022-01-13 | 2022-04-22 | 江西安驰新能源科技有限公司 | Composite positive electrode for all-solid-state lithium ion battery and preparation method of pole piece of composite positive electrode |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115395090A (en) * | 2022-10-10 | 2022-11-25 | 蜂巢能源科技(无锡)有限公司 | Solid electrolyte membrane and preparation method and application thereof |
CN116314598A (en) * | 2023-05-26 | 2023-06-23 | 江苏正力新能电池技术有限公司 | Dry electrode slice and preparation method and application thereof |
CN116314598B (en) * | 2023-05-26 | 2023-09-08 | 江苏正力新能电池技术有限公司 | Dry electrode slice and preparation method and application thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109698354B (en) | Binder, negative electrode slurry using binder, and preparation method and application of negative electrode slurry | |
CN107958993A (en) | Lithium ion battery positive plate coated with composite conductive agent in layered mode and preparation method of lithium ion battery positive plate | |
CN112271285A (en) | Preparation process of lithium ion battery anode slurry | |
CN111987373A (en) | A kind of solid electrolyte coating based on positive electrode protection, positive electrode sheet and preparation method | |
CN106654367A (en) | Preparation method of electrolyte membrane and solid-state lithium battery | |
CN115132961A (en) | A kind of sodium ion battery positive electrode and its preparation method and application | |
CN113363482B (en) | Composite binder for silicon-based negative electrode of lithium ion battery and preparation method and application thereof | |
CN113851609A (en) | Silicon-based negative electrode plate and preparation method thereof, and all-solid-state lithium ion battery | |
CN112151768A (en) | Method for preparing silicon-carbon negative electrode plate by extrusion and calendering and electrode plate | |
CN116470054A (en) | Silicon negative electrode binder and preparation method and application thereof | |
CN114447338A (en) | Positive pole piece slurry and preparation method thereof, lithium ion battery, and vehicle | |
CN115360344A (en) | Composite positive electrode material for sodium ion battery and preparation method thereof | |
CN103606680B (en) | The preparation method of the nitrogenous carbon fibre web negative material of a kind of native graphite compound | |
CN114744151A (en) | A kind of negative pole piece containing binder PAA2, battery and preparation method | |
CN117219774A (en) | Conductive cross-linked binder structured electrode without conductive auxiliary agent, preparation method and application thereof | |
WO2024066186A1 (en) | Binary high-nickel sodium ion battery positive electrode material, preparation method, and application | |
CN115799622A (en) | Composite solid electrolyte particle and preparation method and application thereof | |
CN115295802A (en) | Adhesive, preparation method thereof and application thereof in lithium ion battery | |
CN112952099B (en) | A lithium battery composite positive electrode and preparation method thereof | |
CN116826030B (en) | Composite positive electrode material based on small molecular organic matters and manufacturing method thereof | |
CN104505516A (en) | Positive active material for lithium sulfur battery and preparation method of positive active material | |
CN117012899A (en) | Battery pole piece, preparation method and battery | |
CN114242990B (en) | A polyvinyl alcohol/allyl copolymer interpenetrating network silicon-carbon negative electrode water-based binder and its preparation method and application | |
CN116731635A (en) | Conductive adhesive and preparation method and application thereof | |
CN115347192A (en) | Thick cathode electrode and preparation method and application thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination |