CN108232195A - A kind of pole piece moulding method of the water system ion battery based on polytetrafluoroethylene (PTFE) binding agent - Google Patents
A kind of pole piece moulding method of the water system ion battery based on polytetrafluoroethylene (PTFE) binding agent Download PDFInfo
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- 239000011230 binding agent Substances 0.000 title claims abstract description 46
- 238000000034 method Methods 0.000 title claims abstract description 43
- 239000004810 polytetrafluoroethylene Substances 0.000 title claims abstract description 37
- 229920001343 polytetrafluoroethylene Polymers 0.000 title claims abstract description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 33
- -1 polytetrafluoroethylene Polymers 0.000 title claims abstract description 16
- 238000000465 moulding Methods 0.000 title description 9
- 239000000843 powder Substances 0.000 claims abstract description 91
- 239000002002 slurry Substances 0.000 claims abstract description 41
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 35
- 238000000498 ball milling Methods 0.000 claims abstract description 25
- 239000000919 ceramic Substances 0.000 claims abstract description 24
- 239000012065 filter cake Substances 0.000 claims abstract description 19
- 239000002245 particle Substances 0.000 claims abstract description 15
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 14
- 239000002904 solvent Substances 0.000 claims abstract description 12
- 238000005469 granulation Methods 0.000 claims abstract description 11
- 230000003179 granulation Effects 0.000 claims abstract description 11
- 239000006258 conductive agent Substances 0.000 claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 10
- 238000003825 pressing Methods 0.000 claims abstract description 9
- 150000002500 ions Chemical class 0.000 claims description 23
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 10
- 239000011324 bead Substances 0.000 claims description 10
- 239000007787 solid Substances 0.000 claims description 10
- 239000004744 fabric Substances 0.000 claims description 8
- 239000006229 carbon black Substances 0.000 claims description 7
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims description 6
- 229910001416 lithium ion Inorganic materials 0.000 claims description 6
- 229910021382 natural graphite Inorganic materials 0.000 claims description 6
- 239000011148 porous material Substances 0.000 claims description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 5
- 229910015643 LiMn 2 O 4 Inorganic materials 0.000 claims description 4
- 229910012465 LiTi Inorganic materials 0.000 claims description 4
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 claims description 4
- 229910021383 artificial graphite Inorganic materials 0.000 claims description 4
- 230000018044 dehydration Effects 0.000 claims description 4
- 238000006297 dehydration reaction Methods 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 229910001415 sodium ion Inorganic materials 0.000 claims description 4
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 3
- 229910012851 LiCoO 2 Inorganic materials 0.000 claims description 3
- 229910010707 LiFePO 4 Inorganic materials 0.000 claims description 3
- 229910013290 LiNiO 2 Inorganic materials 0.000 claims description 3
- 239000004917 carbon fiber Substances 0.000 claims description 3
- 229910021389 graphene Inorganic materials 0.000 claims description 3
- 238000007873 sieving Methods 0.000 claims description 2
- 239000008187 granular material Substances 0.000 abstract description 4
- 239000000463 material Substances 0.000 description 17
- 238000004519 manufacturing process Methods 0.000 description 14
- 238000001035 drying Methods 0.000 description 9
- 238000012360 testing method Methods 0.000 description 8
- 238000004146 energy storage Methods 0.000 description 6
- 239000011149 active material Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 4
- 239000008367 deionised water Substances 0.000 description 4
- 229910021641 deionized water Inorganic materials 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- 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 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
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- 239000003513 alkali Substances 0.000 description 2
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- 239000003792 electrolyte Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- 239000011805 ball Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
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- 238000009833 condensation Methods 0.000 description 1
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- 238000004925 denaturation Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000011883 electrode binding agent Substances 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000009830 intercalation Methods 0.000 description 1
- 230000002687 intercalation Effects 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 229910052987 metal hydride Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 229920001021 polysulfide Polymers 0.000 description 1
- 239000005077 polysulfide Substances 0.000 description 1
- 150000008117 polysulfides Polymers 0.000 description 1
- 238000009702 powder compression Methods 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
- H01M4/622—Binders being polymers
- H01M4/623—Binders being polymers fluorinated polymers
-
- 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
- H01M10/36—Accumulators not provided for in groups H01M10/05-H01M10/34
-
- 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
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/043—Processes of manufacture in general involving compressing or compaction
- H01M4/0433—Molding
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/021—Physical characteristics, e.g. porosity, surface area
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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
- H01M2220/00—Batteries for particular applications
- H01M2220/10—Batteries in stationary systems, e.g. emergency power source in plant
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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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- Chemical Kinetics & Catalysis (AREA)
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- Battery Electrode And Active Subsutance (AREA)
Abstract
本发明涉及一种基于聚四氟乙烯粘结剂的水系离子电池的极片成型方法,包括:步骤 1)以水系离子电池电极使用的陶瓷粉体和无机碳源导电剂为原料,使用水作为溶剂,加入聚四氟乙烯作为粘结剂,球磨制得均匀浆料;步骤 2)将所得浆料进行过滤得到滤饼,将得到的滤饼经过进一步烘干得到干燥粉体;步骤 3)将所得到的干燥粉体造粒、过筛,得到粒度均匀的颗粒状粉体;步骤4)将得到的颗粒状粉体采用干压成型的方法批量制备电池极片。本发明采用球磨制作浆料联合造粒的方式,得到的粉体成颗粒状,大大改进粉体因为粘结剂带来的流动性问题,使得极片成型容易控制,由此适合采用干压成型制得厚极片。
The invention relates to a pole piece forming method of a water-based ion battery based on a polytetrafluoroethylene binder, comprising: step 1) using ceramic powder and an inorganic carbon source conductive agent as raw materials for the electrode of the water-based ion battery, and using water as the Solvent, add polytetrafluoroethylene as a binder, and ball mill to obtain a uniform slurry; step 2) filter the obtained slurry to obtain a filter cake, and further dry the obtained filter cake to obtain a dry powder; step 3) The obtained dry powder is granulated and sieved to obtain a granular powder with uniform particle size; Step 4) The obtained granular powder is prepared in batches for battery pole pieces by dry pressing. The present invention adopts the method of ball milling to make slurry and joint granulation, and the obtained powder is in the form of granules, which greatly improves the fluidity problem of the powder caused by the binder, and makes the forming of the pole piece easy to control, so it is suitable for dry pressing. Produce thick pole pieces.
Description
技术领域technical field
本发明涉及一种基于聚四氟乙烯(PTFE)粘结剂作为水系离子电池的极片成型方法,具体涉及一种采用球磨混合,常规干燥造粒,通过粉末自动压片成型机结合自动称量系统控制,批量的极片生产工艺,属于陶瓷粉体材料领域。The invention relates to a pole piece forming method based on polytetrafluoroethylene (PTFE) binder as a water-based ion battery, in particular to a method of mixing by ball milling, conventional drying and granulation, combined with automatic weighing by powder automatic tablet forming machine The system control and batch pole piece production process belong to the field of ceramic powder materials.
背景技术Background technique
低成本的电力储能系统目前在新能源领域的推动下得到迅猛发展,据估计,全球每年对蓄电池的市场需求大约为150亿美元,在工业用蓄电池方面,如:用于UPS、电能质量调节、备用电池等,其市场总量可达50亿美元。在美国、欧洲以及亚洲,正在组建一批生产电力系统储能用的高性能蓄电池企业。近年来,各种新型的蓄电池被相继开发成功,并在电力系统中得到应用。英国的Regenesys Technologies(www.regenesys.com.au/)正在采用PSB(Polysulfide Broe Flow Battery)电池建设一座15MW/120MW·h的储能电站,其净效率约为75%。由于具有高的能量密度和储能效率,目前锂离子电池得到快速发展,在近几年之内锂电池已经占有小型移动设备电源市场份额的50%,但是,生产大容量锂离子电池仍然有一些挑战性的工作要做,主要的障碍在于其居高不下的成本,另一方面是由于它需要特殊的包装和配备必要的内部过充电保护电路。与其他蓄电池相比,水系离子电池的主要优点是储能效率高(接近100%)和使用寿命长(每次放电不超过储能的80%时可充3000次)。并且可望成为成本最低的蓄电池,这也是一种对于环境无害的蓄电池。Low-cost electric energy storage systems are currently being rapidly developed under the impetus of the new energy field. It is estimated that the global annual market demand for batteries is about 15 billion US dollars. In terms of industrial batteries, such as: for UPS, power quality regulation , Backup batteries, etc., the total market volume can reach 5 billion US dollars. In the United States, Europe and Asia, a group of high-performance storage battery companies are being established to produce power system energy storage. In recent years, various new types of storage batteries have been successfully developed and applied in power systems. UK-based Regenesys Technologies (www.regenesys.com.au/) is using PSB (Polysulfide Broe Flow Battery) batteries to build a 15MW/120MW h energy storage power station with a net efficiency of about 75%. Due to its high energy density and energy storage efficiency, lithium-ion batteries are currently developing rapidly. In recent years, lithium-ion batteries have occupied 50% of the market share of small mobile device power supplies. However, there are still some challenges in the production of large-capacity lithium-ion batteries. Challenging work to do, the main hurdle being its high cost, and partly due to the special packaging it requires and the necessary internal overcharge protection circuitry. Compared with other storage batteries, the main advantages of aqueous ion batteries are high energy storage efficiency (nearly 100%) and long service life (rechargeable 3000 times when each discharge does not exceed 80% of the energy storage). And it is expected to be the battery with the lowest cost, which is also a battery that is not harmful to the environment.
以往的镍镉、镍氢电池,超级电容器等,使用的电解液是有机系,电极制备一般采用涂布工艺,在涂布工艺中,粘结剂体系对于电极材料的粘结效果有着很大的影响。粘结剂体系在电极中主要是为了增加电极的粘结强度,防止电极在循环充放电过程中活性物质的脱落。采用厚极片设计的水系离子电池对粘结剂的选择难度很高,粘结剂必须要保证活性物质制浆时的均匀性和安全性,对活性物质颗粒间起到粘结作用。同时具备良好的热稳定性和对电解液稳定。由于采用厚极片设计,所以选用PTFE作为粘结剂具有其他粘结剂不具备的一系列优点,比如使极片粉体具有纤维网状结构,具有高孔隙率,高度可压缩性,优异的抗酸碱腐蚀性,不老化,耐揉变性,不容易掉粉,具很高的抗张强度等特性,但要实现极片的工业化批量生产具有非常大的挑战性。使用PTFE作为水系离子电池的粘结剂体系,常用60%的PTFE乳液作为电极粘结剂,其难点在于搅拌混合过程中通常会产生不可逆的凝结,导致浆料的流动性差,混合均匀性不佳,其次,由于PTFE带来的粉体流动性差问题难以解决,进而导致厚极片的生产难以采用干压成型工艺,例如CN102916186A公开了将负极材料、乙炔黑和粘结剂PTFE混合均匀后擀压成型制备钠离子电池负极,擀压成型难以精确控制极片的质量和厚度,对电池的正负极配比难以控制,电池性能影响较大,电池一致性难以得到保证。故至今鲜有文献报道使用PTFE作为水系离子电池粘结剂厚电池极片设计的大规模工业化生产。In the past, nickel-cadmium, nickel-metal hydride batteries, supercapacitors, etc. used organic electrolytes, and the electrode preparation generally adopted a coating process. In the coating process, the binder system has a great influence on the bonding effect of the electrode materials. influences. The binder system in the electrode is mainly to increase the bonding strength of the electrode and prevent the active material from falling off during the cycle charge and discharge process of the electrode. It is very difficult to choose a binder for the water-based ion battery designed with a thick pole piece. The binder must ensure the uniformity and safety of the active material during pulping, and play a role in bonding the active material particles. At the same time, it has good thermal stability and stability to electrolyte. Due to the thick pole piece design, the choice of PTFE as the binder has a series of advantages that other binders do not have, such as making the pole piece powder have a fiber network structure, high porosity, high compressibility, excellent It is resistant to acid and alkali corrosion, not aging, resistant to kneading and denaturation, not easy to drop powder, and has high tensile strength. However, it is very challenging to realize the industrialized mass production of pole pieces. PTFE is used as the binder system of water-based ion batteries, and 60% PTFE emulsion is commonly used as the electrode binder. The difficulty is that irreversible condensation usually occurs during the stirring and mixing process, resulting in poor fluidity of the slurry and poor mixing uniformity. , secondly, due to the poor fluidity of the powder caused by PTFE, it is difficult to solve the problem, which makes it difficult to adopt the dry pressing molding process for the production of thick pole pieces. It is difficult to accurately control the quality and thickness of the electrode sheet in rolling forming to prepare the negative electrode of sodium ion battery, and it is difficult to control the ratio of positive and negative electrodes of the battery, which has a great impact on battery performance and is difficult to guarantee the consistency of the battery. Therefore, there are few literature reports on the large-scale industrial production of thick battery pole piece design using PTFE as the binder of aqueous ion batteries.
发明内容Contents of the invention
针对现有技术存在的问题,本发明的目的在于提供一种生产周期短、设备廉价、工艺简单、易于控制、适合批量生产的基于聚四氟乙烯粘结剂作为水系离子电池的极片成型方法。Aiming at the problems existing in the prior art, the object of the present invention is to provide a pole piece forming method based on polytetrafluoroethylene binder as an aqueous ion battery with short production cycle, cheap equipment, simple process, easy control and suitable for mass production .
在此,本发明提供一种基于聚四氟乙烯(PTFE)粘结剂作为水系离子电池的极片成型方法,包括:Here, the present invention provides a kind of pole piece forming method based on polytetrafluoroethylene (PTFE) binding agent as aqueous ion battery, comprising:
步骤1)以水系离子电池电极使用的陶瓷粉体和无机碳源导电剂为原料,使用水作为溶剂,加入聚四氟乙烯作为粘结剂,球磨制得均匀浆料;Step 1) Using the ceramic powder used in the electrode of the water-based ion battery and the inorganic carbon source conductive agent as raw materials, using water as a solvent, adding polytetrafluoroethylene as a binder, and ball milling to obtain a uniform slurry;
步骤2)将所得浆料进行过滤得到滤饼,将得到的滤饼经过进一步烘干得到干燥粉体;Step 2) filtering the obtained slurry to obtain a filter cake, and further drying the obtained filter cake to obtain a dry powder;
步骤3)将所得到的干燥粉体造粒、过筛,得到粒度均匀的颗粒状粉体;Step 3) granulating and sieving the obtained dry powder to obtain a granular powder with uniform particle size;
步骤4)将得到的颗粒状粉体采用干压成型的方法批量制备电池极片。Step 4) The obtained granular powder is prepared in batches into battery pole pieces by a method of dry pressing.
本发明采用球磨制作浆料联合造粒的方式,得到的粉体成颗粒状,大大改进粉体因为粘结剂带来的流动性问题,使得极片成型容易控制,由此适合采用干压成型制得厚极片。本发明得到的极片的厚度可为0~3mm。The present invention adopts the method of ball milling to make slurry and joint granulation, and the obtained powder is in the form of granules, which greatly improves the fluidity problem of the powder caused by the binder, and makes the forming of the pole piece easy to control, so it is suitable for dry pressing. Produce thick pole pieces. The thickness of the pole piece obtained by the present invention may be 0-3 mm.
本发明中,所述水系离子电池可为水系钠离子电池或水系锂离子电池。In the present invention, the water-based ion battery may be a water-based sodium-ion battery or a water-based lithium-ion battery.
本发明中,所述极片可为正极极片或负极极片。较佳地,正极极片的陶瓷粉体为LiMn2O4、LiFePO4、LiCoO2、LiNiO2、λ-MnO2、NaMnO2中的至少一种。负极极片的陶瓷粉体为NaTi2(PO4)3、LiTi2(PO4)3中的至少一种。In the present invention, the pole piece can be a positive pole piece or a negative pole piece. Preferably, the ceramic powder of the positive pole piece is at least one of LiMn 2 O 4 , LiFePO 4 , LiCoO 2 , LiNiO 2 , λ-MnO 2 , and NaMnO 2 . The ceramic powder of the negative pole piece is at least one of NaTi 2 (PO4) 3 and LiTi 2 (PO4) 3 .
较佳地,所述导电剂为无机碳源,优选为人造石墨、天然石墨、活性炭、石墨烯、碳黑、碳纤维、介孔碳中的至少一种。Preferably, the conductive agent is an inorganic carbon source, preferably at least one of artificial graphite, natural graphite, activated carbon, graphene, carbon black, carbon fiber, and mesoporous carbon.
较佳地,步骤1)中,粘结剂的含量为陶瓷粉体的0~25wt.%,优选5~20wt.%。Preferably, in step 1), the content of the binder is 0-25wt.%, preferably 5-20wt.%, of the ceramic powder.
较佳地,步骤1)中,所得浆料的固含量为0~80wt.%,优选10~60wt.%。Preferably, in step 1), the solid content of the obtained slurry is 0-80wt.%, preferably 10-60wt.%.
较佳地,步骤1)包括:Preferably, step 1) includes:
将陶瓷粉体、导电剂、溶剂和球磨珠按一定配比倒入球磨桶后,以0~300转/分钟的转速球磨5小时以下得到第一浆料,其中使用氧化锆作为球磨珠,料球比1:(3~6);以及在所得的第一浆料中再加入粘结剂聚四氟乙烯,以0~300转/分钟的转速混合球磨5小时以下。采用分步球磨的方式,可以解决流动性差的问题。After pouring the ceramic powder, conductive agent, solvent and ball milling beads into the ball mill barrel according to a certain ratio, ball milling at a speed of 0 to 300 rpm for less than 5 hours to obtain the first slurry, in which zirconia is used as the ball milling beads. The ball ratio is 1: (3-6); and the binder polytetrafluoroethylene is added to the obtained first slurry, mixed and ball-milled at a speed of 0-300 rpm for less than 5 hours. The problem of poor fluidity can be solved by step-by-step ball milling.
较佳地,步骤2)中,过滤所使用的设备为板框式压滤机或者是离心式过滤设备,选用0~100μm、优选0~50μm孔隙的滤布,脱水至一定湿度后,取得滤布上的固体,进一步使用烘箱烘干,优选地,烘箱设定温度80~150℃。Preferably, in step 2), the equipment used for filtration is a plate and frame filter press or centrifugal filter equipment, and a filter cloth with a pore size of 0-100 μm, preferably 0-50 μm is selected, and after dehydration to a certain humidity, the filter cloth is obtained. The solid on the cloth is further dried in an oven, preferably, the temperature of the oven is set at 80-150°C.
较佳地,步骤3)中,采用机械造粒方式,使用0~5mm,优选0~3mm的网目过筛。制备的粉体成颗粒可以增加粉体的流动性,在极片成型的过程中易于控制精度,易于采用干压成型工艺。Preferably, in step 3), mechanical granulation is adopted, and the mesh is sieved with a mesh size of 0-5 mm, preferably 0-3 mm. Granulating the prepared powder can increase the fluidity of the powder, and it is easy to control the precision in the process of forming the pole piece, and it is easy to adopt the dry pressing forming process.
较佳地,步骤4)中,采用粉体自动压片成型机压片。优选地,采用等体积法压片。Preferably, in step 4), an automatic powder tableting machine is used for tableting. Preferably, an equal volume method is used for tablet compression.
本发明关键点在于,区别于传统的PTFE粘结剂制备水系离子电极极片涂布成型方法,针对厚极片设计,采用球磨制作浆料联合造粒的方式,得到的粉体成颗粒状,大大改进粉体因为粘结剂带来的流动性问题,使得极片成型容易控制,再结合粉体成型过程中的精确称量系统,得到极片质量误差可以控制在2%以内。本发明与现有技术相比,具有以下优点和有益效果:The key point of the present invention is that it is different from the traditional PTFE binder to prepare water-based ionic electrode pole piece coating molding method. It is designed for thick pole piece and adopts the method of ball milling to make slurry and joint granulation, and the obtained powder becomes granular. Greatly improve the fluidity of the powder due to the binder, making the pole piece forming easy to control, combined with the precise weighing system in the powder forming process, the mass error of the pole piece can be controlled within 2%. Compared with the prior art, the present invention has the following advantages and beneficial effects:
1、通过球磨分散,加入粘结剂PTFE,可以实现石墨等活性材料的碳包覆,提高极片孔隙率,增大比表面,提高材料的导电性,极大的提高材料的电化学性能;1. Through ball mill dispersion and adding binder PTFE, carbon coating of graphite and other active materials can be realized, the porosity of the pole piece can be increased, the specific surface area can be increased, the conductivity of the material can be improved, and the electrochemical performance of the material can be greatly improved;
2、通过机械造粒方式,可以得到尺寸分布均匀的颗粒,有利于提高粉体的流动性能,为粉体压片成型创造条件;2. Through mechanical granulation, particles with uniform size distribution can be obtained, which is conducive to improving the flow performance of the powder and creating conditions for powder compression molding;
3、粉末自动成型设备,结合精确的称量系统,可以有效的控制极片的质量,保证极片的一致性,另外,采用干压成型设备可以保证极片压力可调,厚度可控,极片孔隙率各方面参数都可以调整。极片成型成品率高,适合批量化生产;3. Powder automatic molding equipment, combined with an accurate weighing system, can effectively control the quality of the pole piece and ensure the consistency of the pole piece. In addition, the use of dry pressing molding equipment can ensure that the pressure of the pole piece is adjustable, the thickness is controllable, and the pole piece is extremely stable. All parameters of sheet porosity can be adjusted. Pole piece molding yield is high, suitable for mass production;
4、本发明生产周期短、设备廉价、工艺简单、易于控制,具有显著的实用价值和良好的应用前景。4. The invention has short production cycle, cheap equipment, simple process and easy control, and has remarkable practical value and good application prospect.
附图说明Description of drawings
图1为本发明一个示例的批量生产水系离子电池极片的流程图;Fig. 1 is the flow chart of the batch production water system ion battery pole piece of an example of the present invention;
图2为实施例1经过造粒后得到的粉体颗粒的SEM图;Fig. 2 is the SEM image of the powder particles obtained after granulation in Example 1;
图3为实施例1批量生产的陶瓷极片的实物图,其中左图为测试极片的厚度,右图为测试极片的尺寸;Fig. 3 is the physical figure of the ceramic pole piece of embodiment 1 batch production, and wherein the left figure is the thickness of test pole piece, and the right figure is the size of test pole piece;
图4为实施例1批量制备的极片组装成的单体电池的充放电曲线图。FIG. 4 is a charge-discharge curve diagram of a single battery assembled from pole pieces prepared in batches in Example 1. FIG.
具体实施方式Detailed ways
以下结合附图和下述实施方式进一步说明本发明,应理解,附图及下述实施方式仅用于说明本发明,而非限制本发明。此外,本发明中提及的范围值的下限值为0的,优选为不包括0。The present invention will be further described below in conjunction with the drawings and the following embodiments. It should be understood that the drawings and the following embodiments are only used to illustrate the present invention rather than limit the present invention. In addition, the lower limit value of the range value mentioned in the present invention is 0, preferably excluding 0.
本发明提供一种基于聚四氟乙烯(PTFE)粘结剂作为水系离子电池的极片成型方法。本发明中,水系离子电池是指具有水系电解液的离子电池,例如水系钠离子电池、水系锂离子电池等。电池极片可以是正极极片,也可以是负极极片。本发明尤其适用于厚极片的制备,例如其厚度可为0~3mm。The invention provides a method for forming pole pieces based on polytetrafluoroethylene (PTFE) binder as an aqueous ion battery. In the present invention, the water-based ion battery refers to an ion battery with a water-based electrolyte, such as a water-based sodium-ion battery, a water-based lithium-ion battery, and the like. The battery pole piece can be a positive pole piece or a negative pole piece. The present invention is especially suitable for the preparation of thick pole pieces, for example, the thickness can be 0-3mm.
本发明使用几种特定的原料,通过分步球磨方法获得具有一定黏度和粒径的浆料。通过对浆料的进一步干燥处理,结合造粒工艺,得到混合均匀,流动性较好的粉体,在特定的压片工艺下批量化生产极片。图1为本发明一个示例的批量生产水系离子电池极片的流程图。以下参照图1说明本发明。The invention uses several specific raw materials, and obtains slurry with certain viscosity and particle size through a stepwise ball milling method. Through further drying of the slurry, combined with the granulation process, a uniformly mixed and fluid powder is obtained, and the pole pieces are mass-produced under a specific tableting process. Fig. 1 is a flow chart of mass production of pole pieces of aqueous ion batteries according to an example of the present invention. The present invention will be described below with reference to FIG. 1 .
首先,进行混料,制得浆料。具体而言,以水系离子电池正负电极使用的陶瓷粉体、导电剂(例如碳源)等活性物质粉体为原料粉体,使用水作为溶剂,加入粘结剂聚四氟乙烯(PTFE),球磨制得均匀浆料。First, mixing is carried out to obtain a slurry. Specifically, active material powders such as ceramic powders and conductive agents (such as carbon sources) used in the positive and negative electrodes of water-based ion batteries are used as raw material powders, water is used as a solvent, and a binder polytetrafluoroethylene (PTFE) is added. , ball milled to obtain a uniform slurry.
正极陶瓷粉体可采用本领域常用的钠(或锂)离子可嵌入和脱出的具有相对高的嵌/脱电位平台的材料,如LiMn2O4、LiFePO4、LiCoO2、LiNiO2、λ-MnO2、NaMnO2中的一种或几种。负极陶瓷粉体可采用钠(或锂)离子可嵌入和脱出的具有相对低的嵌/脱电位平台的材料,如NaTi2(PO4)3、LiTi2(PO4)3中的一种或几种。原料陶瓷粉体纯度可为工业级,可自己合成或者商业购买。The positive electrode ceramic powder can be made of materials commonly used in this field that can intercalate and deintercalate sodium (or lithium) ions, such as LiMn 2 O 4 , LiFePO 4 , LiCoO 2 , LiNiO 2 , λ- One or more of MnO 2 and NaMnO 2 . The negative electrode ceramic powder can be made of a material with a relatively low intercalation/extraction potential platform that can intercalate and deintercalate sodium (or lithium) ions, such as one or more of NaTi 2 (PO4) 3 and LiTi 2 (PO4) 3 . The purity of the raw ceramic powder can be industrial grade, and can be synthesized by oneself or purchased commercially.
碳源可为无机碳源,优选为人造石墨、天然石墨、活性炭、石墨烯、碳黑、碳纤维、介孔碳其中的任意一种或几种。陶瓷粉体和导电剂的质量比可为(50~95):(50~5)。The carbon source can be an inorganic carbon source, preferably any one or several of artificial graphite, natural graphite, activated carbon, graphene, carbon black, carbon fiber, and mesoporous carbon. The mass ratio of the ceramic powder and the conductive agent may be (50-95): (50-5).
本发明使用聚四氟乙烯(PTFE)作为粘结剂,其可以使极片粉体具有纤维网状结构,具有高孔隙率,高度可压缩性,优异的抗酸碱腐蚀性,不老化,耐揉变性,不容易掉粉,具很高的抗张强度等特性。粘结剂含量可为原料粉体(包含陶瓷粉体和导电剂)的0~25wt.%,优选5~20wt.%。通过改变粘结剂的用量,可以调节得到的极片的孔隙率。例如,在上述范围内,随着粘结剂的用量的增加,极片的孔隙率也增加。The present invention uses polytetrafluoroethylene (PTFE) as a binder, which can make the pole piece powder have a fiber network structure, high porosity, high compressibility, excellent acid and alkali corrosion resistance, no aging, and Kneading denatured, not easy to drop powder, with high tensile strength and other characteristics. The binder content can be 0-25wt.%, preferably 5-20wt.%, of the raw material powder (including ceramic powder and conductive agent). By changing the amount of the binder, the porosity of the obtained pole piece can be adjusted. For example, within the above range, as the amount of binder increases, the porosity of the pole piece also increases.
球磨时,可使用氧化锆作为球磨珠,料球比可为1:(3-6)。所得浆料的固含量为0~80wt.%,优选为10~60wt.%。浆料的黏度可为0~1000Pa.s。For ball milling, zirconia can be used as ball milling beads, and the material-to-ball ratio can be 1:(3-6). The solid content of the obtained slurry is 0-80wt.%, preferably 10-60wt.%. The viscosity of the slurry can be 0-1000Pa.s.
在一个示例中,通过分步球磨方法获得具有一定黏度和粒径的浆料。具体而言,将粉体、溶剂、球磨珠按一定配比倒入球磨桶后,以0~300转/分钟的转速球磨0~5小时得到第一浆料;以及在所得的第一浆料中再加入粘结剂PTFE,以0~300转/分钟的转速混合球磨0~5小时。分步球磨相较于一步球磨,可以球磨均匀,有效分散PTFE粘结剂。In one example, the slurry with certain viscosity and particle size is obtained by step ball milling method. Specifically, after pouring the powder, solvent, and ball milling beads into a ball mill barrel according to a certain ratio, ball milling at a speed of 0 to 300 rpm for 0 to 5 hours to obtain the first slurry; and in the obtained first slurry Then add the binder PTFE, mix and ball mill for 0-5 hours at a speed of 0-300 rpm. Compared with one-step ball milling, step-by-step ball milling can be evenly milled and effectively disperse PTFE binder.
接着,对浆料进行干燥。先将浆料进行过滤得到滤饼,为进一步粉体干燥降低能耗,然后将得到的滤饼经过进一步烘箱干燥。浆料含有粘结剂,可以控制滤布的孔隙来控制浆料的过滤脱水。可以使用板框式压滤设备或者离心式过滤设备。滤布孔隙可为0~100μm。脱水至一定湿度后,取得滤布上的固体,进一步使用烘箱烘干得到干燥粉体。在烘干过程中,较佳地,干燥箱设定温度80~150℃(溶剂挥发温度)。干燥时间可为0~48小时。Next, the slurry is dried. The slurry is first filtered to obtain a filter cake to reduce energy consumption for further powder drying, and then the obtained filter cake is further dried in an oven. The slurry contains a binder, which can control the pores of the filter cloth to control the filtration and dehydration of the slurry. Plate and frame filter press equipment or centrifugal filter equipment can be used. The pores of the filter cloth can be 0-100 μm. After dehydration to a certain humidity, the solid on the filter cloth is obtained, and further dried in an oven to obtain a dry powder. During the drying process, preferably, the temperature of the drying oven is set at 80-150° C. (solvent volatilization temperature). The drying time may range from 0 to 48 hours.
将干燥粉体造粒、震动过筛,得到颗粒状粉体。可以使用0~3mm的网目过筛。由此,可以得到流动性较好的粉体颗粒,便于进一步极片成型。图2示出本发明一个示例中造粒后的粉体的SEM,可以看出粉体成颗粒状。The dry powder is granulated, shaken and sieved to obtain a granular powder. It can be sieved with a mesh of 0-3mm. In this way, powder particles with better fluidity can be obtained, which is convenient for further pole piece forming. Fig. 2 shows the SEM of the granulated powder in an example of the present invention, it can be seen that the powder is in the form of granules.
将得到的颗粒状粉体进一步压片成型,制得极片。本发明中,可采用干压成型的方法,以粉末成型压片机自动化批量制备电池正负极极片。由此,能够有效地控制极片的厚度和强度,批量化得到质量均一的极片。压片时,可使用自制的特定模具,满足生产需要的尺寸。调节双向冲头的压力以控制极片成型厚度和机械强度。极片孔隙率可通过粘结剂的用量来调节。例如压力可控制在0~300MPa。得到的极片的厚度可为0~3mm,其强度可为0~10Mpa。极片孔隙率可在10~70%范围内可调。The obtained granular powder is further compressed into tablets to obtain pole pieces. In the present invention, the method of dry pressing can be adopted, and the positive and negative pole pieces of the battery can be prepared in batches automatically with a powder forming tablet press. Thus, the thickness and strength of the pole pieces can be effectively controlled, and pole pieces with uniform quality can be obtained in batches. When compressing tablets, a self-made specific mold can be used to meet the size required for production. Adjust the pressure of the two-way punch to control the forming thickness and mechanical strength of the pole piece. The porosity of pole piece can be adjusted by the amount of binder. For example, the pressure can be controlled at 0-300MPa. The thickness of the obtained pole piece can be 0-3mm, and its strength can be 0-10Mpa. The porosity of pole piece can be adjusted in the range of 10-70%.
本发明工艺简单、成本低,球磨均匀,粉体分散度好。采用压滤式或者离心式干燥方式得到的粉体湿度可控,为进一步粉体干燥降低能耗,有利于低成本的大规模生产制备。而且制备的粉体采用分步球磨联合造粒方式解决了粉体因为粘结剂而流动性差的问题,为极片的批量化生产奠定基础,也为电池的性能提供保证,使得电池的商业化应用可以实现。The invention has the advantages of simple process, low cost, uniform ball milling and good powder dispersion. The humidity of the powder obtained by filter press or centrifugal drying is controllable, which reduces energy consumption for further powder drying and is conducive to large-scale production and preparation at low cost. Moreover, the prepared powder adopts the step-by-step ball milling combined granulation method to solve the problem of poor fluidity of the powder due to the binder, which lays the foundation for the mass production of the pole piece, and also provides a guarantee for the performance of the battery, making the commercialization of the battery application can be achieved.
下面进一步例举实施例以详细说明本发明。同样应理解,以下实施例只用于对本发明进行进一步说明,不能理解为对本发明保护范围的限制,本领域的技术人员根据本发明的上述内容作出的一些非本质的改进和调整均属于本发明的保护范围。下述示例具体的工艺参数等也仅是合适范围中的一个示例,即本领域技术人员可以通过本文的说明做合适的范围内选择,而并非要限定于下文示例的具体数值。Examples are given below to describe the present invention in detail. It should also be understood that the following examples are only used to further illustrate the present invention, and should not be construed as limiting the protection scope of the present invention. Some non-essential improvements and adjustments made by those skilled in the art according to the above contents of the present invention all belong to the present invention scope of protection. The specific process parameters and the like in the following examples are only examples of suitable ranges, that is, those skilled in the art can make a selection within a suitable range through the description herein, and are not limited to the specific values exemplified below.
实施例1Example 1
将60g正极陶瓷粉体λ-MnO2,无机碳源10g炭黑,15g活性碳,10g天然石墨粉体为原料,使用去离子水作为溶剂,控制粉体的固含量为30wt.%,使用氧化锆作为球磨珠,料球比1:5,粗磨机高速120转/每分钟球磨2h获得均匀的浆料。继续加入5wt.%PTFE粘结剂(加入的粘结剂量不同对孔隙的影响也不一样,见表1),进一步以300转/分钟的转速球磨5h后倒出浆料。将得到的浆料采用板框式压滤设备过滤,得到滤饼,将得到的滤饼经过进一步烘箱烘干,设定温度110℃,放置12h,得到干燥的块状物料,将所得到的干燥物料进行机械造粒,使用3mm网目震动过筛,得到粒度均匀的颗粒状粉体,便于进一步极片成型,将得到的颗粒状粉体进一步采用粉末成型压片机自动化批量制备电池正极极片,压力为200MPa。Use 60g of positive electrode ceramic powder λ-MnO 2 , 10g of carbon black as an inorganic carbon source, 15g of activated carbon, and 10g of natural graphite powder as raw materials, use deionized water as a solvent, and control the solid content of the powder to 30wt.%. Zirconium is used as ball milling beads, the ratio of material to ball is 1:5, and the coarse mill is milled at a high speed of 120 rpm/min for 2 hours to obtain a uniform slurry. Continue to add 5wt.% PTFE binder (different amounts of binder added have different effects on pores, see Table 1), further ball mill at 300 rpm for 5 hours, and then pour out the slurry. Filter the obtained slurry with plate-and-frame filter press equipment to obtain a filter cake, and further oven-dry the obtained filter cake, set the temperature at 110°C, and place it for 12 hours to obtain a dry block material, and dry the obtained filter cake The material is mechanically granulated, and sieved by vibration with a 3mm mesh to obtain a granular powder with uniform particle size, which is convenient for further electrode sheet forming. The obtained granular powder is further automatically prepared in batches for battery positive electrodes using a powder forming tablet press. , the pressure is 200MPa.
图2为实施例1经过造粒后得到的粉体颗粒的SEM图,可以看出粉体成颗粒状,且粒径较为均匀。图3为实施例1批量生产的陶瓷极片的实物图,可以看出极片表面光滑平整,厚度一致性好。经测试,极片的厚度为2.486mm,强度为5.2Mpa。Fig. 2 is an SEM image of the powder particles obtained after granulation in Example 1. It can be seen that the powder is in the form of granules, and the particle size is relatively uniform. Fig. 3 is a physical picture of the ceramic pole piece mass-produced in Example 1. It can be seen that the surface of the pole piece is smooth and flat, and the thickness is consistent. After testing, the pole piece has a thickness of 2.486mm and a strength of 5.2Mpa.
表1为实施例1中改变粘结剂的用量得到的极片的孔隙率,可知加入的粘结剂量不同对孔隙的影响也不一样;Table 1 shows the porosity of the pole piece obtained by changing the amount of binder used in Example 1. It can be seen that different amounts of binder added have different effects on the pores;
表1不同PTFE含量对应的极片孔隙率Table 1 Porosity of pole piece corresponding to different PTFE contents
参照实施例1将批量制备的极片组装成单体电池进行测试,测试结果为:在0.1C倍率下,电池正常放电容量达到30Ah(参见图4),满足水系离子电池性能要求。Referring to Example 1, the pole pieces prepared in batches were assembled into a single battery for testing. The test result was: at a rate of 0.1C, the normal discharge capacity of the battery reached 30Ah (see FIG. 4 ), meeting the performance requirements of the water-based ion battery.
实施例2Example 2
将70g正极陶瓷粉体LiMn2O4,无机碳源5g炭黑,5g活性碳,10g人造石墨粉体为原料,使用去离子水作为溶剂,控制粉体的固含量为30wt.%,使用氧化锆作为球磨珠,料球比1:6,粗磨机高速200转/每分钟球磨4h获得均匀的浆料。继续加入10wt.%PTFE粘结剂,进一步以250转/分钟的转速球磨3h后倒出浆料。将得到的浆料采用板框式压滤设备过滤,得到滤饼,将得到的滤饼经过进一步烘箱烘干,设定温度110℃,放置12h,得到干燥的块状物料,将所得到的干燥物料进行摇摆式颗粒机造粒,使用1mm网目震动过筛,得到粒度均匀的颗粒状粉体,便于进一步极片成型,将得到的颗粒状粉体进一步采用粉末成型压片机自动化批量制备电池正极极片,成型压力为300MPa。70g positive electrode ceramic powder LiMn 2 O 4 , inorganic carbon source 5g carbon black, 5g activated carbon, and 10g artificial graphite powder were used as raw materials, deionized water was used as a solvent, and the solid content of the powder was controlled to 30wt.%. Zirconium is used as ball milling beads, the ratio of material to ball is 1:6, and the coarse mill is milled at a high speed of 200 rpm/min for 4 hours to obtain a uniform slurry. Continue to add 10wt.% PTFE binder, further ball mill at 250 rpm for 3 hours, and pour out the slurry. Filter the obtained slurry with plate-and-frame filter press equipment to obtain a filter cake, and further oven-dry the obtained filter cake, set the temperature at 110°C, and place it for 12 hours to obtain a dry block material, and dry the obtained The material is granulated by a swinging granulator, vibrating and sieved with a 1mm mesh to obtain a granular powder with uniform particle size, which is convenient for further electrode sheet forming, and the obtained granular powder is further automatically prepared in batches by a powder forming tablet press machine. Positive pole piece, molding pressure is 300MPa.
经测试,极片的厚度为2.512mm,强度为8.6Mpa,孔隙率为35.86%。After testing, the pole piece has a thickness of 2.512mm, a strength of 8.6Mpa, and a porosity of 35.86%.
实施例3Example 3
将60g负极陶瓷粉体NaTi2(PO4)3,无机碳源10g炭黑,15g天然石墨粉体为原料,使用去离子水作为溶剂,控制粉体的固含量为60wt.%,使用氧化锆作为球磨珠,料球比1:3,粗磨机高速100转/每分钟球磨5h获得均匀的浆料。继续加入15wt.%PTFE粘结剂,进一步以300转/分钟的转速球磨2h后倒出浆料。将得到的浆料采用板框式压滤设备过滤,得到滤饼,将得到的滤饼经过进一步烘箱烘干,设定温度110℃,放置12h,得到干燥的块状物料,将所得到的干燥物料进行机械造粒,使用2mm网目震动过筛,得到粒度均匀的颗粒状粉体,便于进一步极片成型,将得到的颗粒状粉体进一步采用粉末成型压片机自动化批量制备电池负极极片,压力为300MPa。With 60g of negative electrode ceramic powder NaTi 2 (PO4) 3 , 10g of carbon black as an inorganic carbon source, and 15g of natural graphite powder as raw materials, use deionized water as a solvent, control the solid content of the powder to 60wt.%, and use zirconia as Ball milling beads, the ratio of material to ball is 1:3, and the coarse mill is milled at a high speed of 100 rpm/min for 5 hours to obtain a uniform slurry. Continue to add 15wt.% PTFE binder, further ball mill at 300 rpm for 2 hours, and pour out the slurry. Filter the obtained slurry with plate-and-frame filter press equipment to obtain a filter cake, and further oven-dry the obtained filter cake, set the temperature at 110°C, and place it for 12 hours to obtain a dry block material, and dry the obtained filter cake The material is mechanically granulated, and sieved by vibration with a 2mm mesh to obtain a granular powder with uniform particle size, which is convenient for further electrode sheet forming. The obtained granular powder is further automatically prepared in batches for battery negative electrodes using a powder forming tablet press. , the pressure is 300MPa.
经测试,极片的厚度为2.623mm,强度为8.4Mpa,孔隙率为40.5%。After testing, the pole piece has a thickness of 2.623mm, a strength of 8.4Mpa, and a porosity of 40.5%.
实施例4Example 4
将50g负极陶瓷粉体LiTi2(PO4)3,无机碳源20g炭黑,10g天然石墨粉体为原料,使用去离子水作为溶剂,控制粉体的固含量为50wt.%,使用氧化锆作为球磨珠,料球比1:5,粗磨机高速150转/每分钟球磨3h获得均匀的浆料。继续加入20wt.%PTFE粘结剂,进一步以200转/分钟的转速球磨3h后倒出浆料。将得到的浆料采用板框式压滤设备过滤,得到滤饼,将得到的滤饼经过进一步烘箱烘干,设定温度100℃,放置24h,得到干燥的块状物料,将所得到的干燥物料进行机械造粒,使用2mm网目震动过筛,得到粒度均匀的颗粒状粉体,便于进一步极片成型,将得到的颗粒状粉体进一步采用粉末成型压片机自动化批量制备电池负极极片,成型压力为100MPa。With 50g of negative electrode ceramic powder LiTi 2 (PO4) 3 , 20g of carbon black as an inorganic carbon source, and 10g of natural graphite powder as raw materials, use deionized water as a solvent, control the solid content of the powder to 50wt.%, and use zirconia as Ball mill the beads, the ratio of material to ball is 1:5, and the high speed of the coarse mill is 150 rpm/min for 3 hours to obtain a uniform slurry. Continue to add 20wt.% PTFE binder, further ball mill at 200 rpm for 3 hours, and pour out the slurry. Filter the obtained slurry with plate-and-frame filter press equipment to obtain a filter cake, and further oven-dry the obtained filter cake, set the temperature at 100°C, and place it for 24 hours to obtain a dry block material, and dry the obtained filter cake The material is mechanically granulated, and sieved by vibration with a 2mm mesh to obtain a granular powder with uniform particle size, which is convenient for further electrode sheet forming. The obtained granular powder is further automatically prepared in batches for battery negative electrodes using a powder forming tablet press. , The molding pressure is 100MPa.
经测试,极片的厚度为2.684mm,强度为4.5Mpa,孔隙率为57.6%。After testing, the pole piece has a thickness of 2.684mm, a strength of 4.5Mpa and a porosity of 57.6%.
产业应用性:本发明的方法降低了使用PTFE粘结剂作为水系离子电池极片成型工艺的生产难度和生产成本,提高了生产的极片电化学性能,为水系离子电池的商业化生产奠定基础。Industrial Applicability: The method of the present invention reduces the production difficulty and production cost of using PTFE binder as the pole piece forming process of the water-based ion battery, improves the electrochemical performance of the produced pole piece, and lays the foundation for the commercial production of the water-based ion battery .
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