CN116169301A - Current collector for sodium ion secondary battery, preparation method and equipment - Google Patents
Current collector for sodium ion secondary battery, preparation method and equipment Download PDFInfo
- Publication number
- CN116169301A CN116169301A CN202211612519.6A CN202211612519A CN116169301A CN 116169301 A CN116169301 A CN 116169301A CN 202211612519 A CN202211612519 A CN 202211612519A CN 116169301 A CN116169301 A CN 116169301A
- Authority
- CN
- China
- Prior art keywords
- secondary battery
- ion secondary
- sodium ion
- optionally
- current collector
- 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.)
- Granted
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
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/665—Composites
- H01M4/667—Composites in the form of layers, e.g. coatings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
-
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Composite Materials (AREA)
- Nanotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Physics & Mathematics (AREA)
- Crystallography & Structural Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Cell Electrode Carriers And Collectors (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
本发明涉及钠离子二次电池,具体涉及一种钠离子二次电池用集流体及制备方法与设备。钠离子二次电池正极集流体包括中间层金属箔,和分别位于所述中间层两侧的涂层;所述涂层含有纳米纤维素和导电剂。本发明钠离子二次电池正极集流体集流体隔绝了钠离子正极材料与铝箔之间的接触,克服了现有钠离子二次电池中出现的正极材料与铝箔之间因为发生化学反应导致的极片压实密度低,成品电池容量的降低及寿命降低等问题。
The invention relates to a sodium ion secondary battery, in particular to a current collector for a sodium ion secondary battery, a preparation method and equipment. The positive current collector of the sodium ion secondary battery comprises a metal foil of an intermediate layer, and coatings respectively located on both sides of the intermediate layer; the coating contains nanocellulose and a conductive agent. The positive electrode current collector of the sodium ion secondary battery of the present invention isolates the contact between the positive electrode material of the sodium ion and the aluminum foil, and overcomes the polarity caused by the chemical reaction between the positive electrode material and the aluminum foil in the existing sodium ion secondary battery. The compaction density of the sheet is low, the capacity of the finished battery is reduced, and the service life is reduced.
Description
技术领域technical field
本发明涉及钠离子二次电池,具体涉及一种钠离子二次电池用集流体及制备方法与设备。The invention relates to a sodium ion secondary battery, in particular to a current collector for a sodium ion secondary battery, a preparation method and equipment.
背景技术Background technique
21世纪,锂电池被应用于手机、电脑、穿戴设备、电动汽车、二轮自行车、电动工具、路灯等众多领域。近年来,锂资源的消耗呈现出使用量大、消耗速度快,并且锂的生产量增长无法满足消耗量增长的现象:这是因为:一是锂资源是有限的,主要以锂辉石矿石和盐湖锂状态存在,二是冬季盐湖锂无法提锂。对比之下,钠来源广泛、储量丰富,钠的储量是锂的420倍,价格远低于锂。近年来,随着锂价疯狂上涨,钠离子电池有望比锂离子电池低30-50%的成本而受到广泛关注,特别是在储能领域、混合动力领域、替代铅酸电池领域,钠离子电池具有诱人的应用前景。In the 21st century, lithium batteries are used in many fields such as mobile phones, computers, wearable devices, electric vehicles, two-wheeled bicycles, electric tools, and street lamps. In recent years, the consumption of lithium resources has shown a phenomenon of large usage and fast consumption, and the growth of lithium production cannot meet the growth of consumption: this is because: first, lithium resources are limited, mainly spodumene ore and The state of lithium in salt lake exists, and the second is that lithium in salt lake cannot be extracted in winter. In contrast, sodium has a wide range of sources and abundant reserves. The reserve of sodium is 420 times that of lithium, and its price is much lower than that of lithium. In recent years, with the crazy rise in lithium prices, sodium-ion batteries are expected to cost 30-50% lower than lithium-ion batteries and have attracted widespread attention, especially in the field of energy storage, hybrid power, and the field of replacing lead-acid batteries. It has attractive application prospects.
目前,钠离子电池正极电极制备方法:将Na3V2(PO4)3、NaFe1/3Ni1/3Mn1/3O3、普鲁士蓝三种材料中的一种与导电剂、粘结剂制备成浆料涂布于铝箔上,再经烘干、碾压、分切等工序制备而成。At present, the preparation method of the positive electrode of the sodium ion battery is: one of the three materials Na 3 V 2 (PO 4 ) 3 , NaFe 1/3 Ni 1/3 Mn 1/3 O 3 , and Prussian blue is mixed with a conductive agent, an adhesive The binder is prepared as a slurry and coated on an aluminum foil, and then prepared by drying, rolling, slitting and other processes.
与锂离子二次电池正极材料相比,钠离子二次电池正极材料的碱性更高,正极材料与铝箔之间因为接触发生一定的化学反应,导致碾压工序正极片压实密度降低、正极材料损失从而成品钠离子二次电池容量的降低、电池循环寿命降低。Compared with the positive electrode material of lithium ion secondary battery, the alkalinity of the positive electrode material of sodium ion secondary battery is higher, and a certain chemical reaction occurs between the positive electrode material and the aluminum foil due to contact, which leads to a decrease in the compaction density of the positive electrode sheet during the rolling process, and the positive electrode Material loss leads to a reduction in the capacity of the finished sodium ion secondary battery and a reduction in the cycle life of the battery.
发明内容Contents of the invention
本发明旨在至少在一定程度上解决现有技术中的技术问题之一。The present invention aims at solving one of the technical problems of the prior art at least to a certain extent.
本发明提供一种钠离子二次电池正极集流体及制备方法与设备,该集流体隔绝了钠离子正极材料与铝箔之间的接触,克服了现有钠离子二次电池中出现的正极材料与铝箔之间因为发生化学反应导致的极片压实密度低,成品电池容量的降低及寿命降低等问题。The present invention provides a positive electrode current collector of a sodium ion secondary battery, a preparation method and equipment. The current collector isolates the contact between the positive electrode material of the sodium ion and the aluminum foil, and overcomes the problem of the positive electrode material and the aluminum foil in the existing sodium ion secondary battery. Due to the chemical reaction between the aluminum foils, the compaction density of the pole pieces is low, the capacity of the finished battery is reduced, and the service life is reduced.
一种钠离子二次电池正极集流体,包括中间层金属箔,和分别位于所述中间层两侧的涂层;所述涂层含有纳米纤维素和导电剂。A sodium ion secondary battery cathode current collector comprises a metal foil in an intermediate layer and coatings respectively located on both sides of the intermediate layer; the coating contains nanocellulose and a conductive agent.
本发明的集流体采用三层结构,上下两层为涂层,中间为金属箔(例如铝箔);涂层中的纳米纤维素组分阻止正极材料与铝箔接触,杜绝两者之间发生化学反应;由于纳米纤维素不导电,涂层中加入了高导电组分,实现了正极材料与集流体之间的电子导通。The current collector of the present invention adopts a three-layer structure, the upper and lower layers are coatings, and the middle is metal foil (such as aluminum foil); the nanocellulose component in the coating prevents the contact between the positive electrode material and the aluminum foil, and prevents chemical reactions between the two ; Since the nanocellulose is non-conductive, a highly conductive component is added to the coating to realize the electronic conduction between the positive electrode material and the current collector.
根据本发明实施例,所述金属箔选自铝箔或铜箔。可选地,所述金属箔的厚度为10-20μm,例如15μm。According to an embodiment of the present invention, the metal foil is selected from aluminum foil or copper foil. Optionally, the metal foil has a thickness of 10-20 μm, such as 15 μm.
根据本发明实施例,所述涂层的厚度为0.5-5μm,例如1-2μm。According to an embodiment of the present invention, the thickness of the coating is 0.5-5 μm, such as 1-2 μm.
根据本发明实施例,所述涂层中含有纳米纤维素30-75wt%,可选为60-72wt%;所述涂层中含有导电剂10-40wt%,可选为25-37wt%。According to an embodiment of the present invention, the coating contains 30-75wt% of nanocellulose, optionally 60-72wt%, and the coating contains 10-40wt% of a conductive agent, optionally 25-37wt%.
根据本发明实施例,所述纳米纤维素选自纤维素纳米晶体、纤维素纳米纤丝中的一种或两种。According to an embodiment of the present invention, the nanocellulose is selected from one or both of cellulose nanocrystals and cellulose nanofibrils.
可选地,所述纤维素纳米晶体的直径5-70nm,长度25-300nm;优选直径5-20nm,长度25-100nm;进一步优选直径15-20nm,长度35-45nm。Optionally, the cellulose nanocrystals have a diameter of 5-70 nm and a length of 25-300 nm; preferably a diameter of 5-20 nm and a length of 25-100 nm; more preferably a diameter of 15-20 nm and a length of 35-45 nm.
可选地,所述纤维素纳米纤丝的直径5-60nm,长度100-3000nm;优选直径5-20nm,长度500-1500nm;进一步优选直径5-10nm,长度500-650nm。Optionally, the cellulose nanofibrils have a diameter of 5-60 nm and a length of 100-3000 nm; preferably a diameter of 5-20 nm and a length of 500-1500 nm; more preferably a diameter of 5-10 nm and a length of 500-650 nm.
在一些实施例,所述纳米纤维素是与纤维素纳米纤丝的混合物,二者质量比为1:1;纤维素纳米晶体直径15-20nm,长度35-45nm;纤维素纳米纤丝直径5-10nm,长度500-650nm。In some embodiments, the nanocellulose is a mixture with cellulose nanofibrils, the mass ratio of the two is 1:1; the diameter of cellulose nanocrystals is 15-20 nm, and the length is 35-45 nm; the diameter of cellulose nanofibrils is 5 nm. -10nm, length 500-650nm.
根据本发明实施例,所述导电剂选自炭黑、乙炔黑、碳纳米管、科琴黑、碳纤维中的一种或者几种;优选乙炔黑与碳纳米管,二者质量比为1:1。According to an embodiment of the present invention, the conductive agent is selected from one or more of carbon black, acetylene black, carbon nanotubes, Ketjen black, and carbon fibers; preferably acetylene black and carbon nanotubes, the mass ratio of the two is 1: 1.
根据本发明实施例,所述涂层中还含有粘结剂,含量可选为1-5wt%,进一步可选为2-5wt%。According to an embodiment of the present invention, the coating further contains a binder, the content of which may be 1-5wt%, and further may be 2-5wt%.
根据本发明实施例,所述粘结剂是聚偏氟乙烯(PVDF),优选分子量为80-120万,例如100万。研究发现,若聚偏氟乙烯的分子量过低则粘结性较差,分子量过高则溶解困难。According to an embodiment of the present invention, the binder is polyvinylidene fluoride (PVDF), preferably with a molecular weight of 800,000-1.2 million, such as 1 million. Studies have found that if the molecular weight of polyvinylidene fluoride is too low, the cohesiveness will be poor, and if the molecular weight is too high, it will be difficult to dissolve.
根据本发明实施例,所述涂层中还含有分散剂,含量可选为0.5-3wt%,进一步可选为1-3wt%。According to an embodiment of the present invention, the coating further contains a dispersant, the content of which may be 0.5-3wt%, and further may be 1-3wt%.
根据本发明实施例,所述分散剂是聚乙烯吡咯烷酮(PVP),优选分子量为60-120万,例如80万。研究发现,若聚乙烯吡咯烷酮的分子量过低则分散性较差,分子量过高则溶解困难。According to an embodiment of the present invention, the dispersant is polyvinylpyrrolidone (PVP), preferably with a molecular weight of 600,000-1.2 million, such as 800,000. Studies have found that if the molecular weight of polyvinylpyrrolidone is too low, the dispersibility will be poor, and if the molecular weight is too high, it will be difficult to dissolve.
根据本发明实施例,制备所述涂层的原料还包括溶剂,可选为N-甲基吡咯烷酮(NMP)。通常情况下,经干燥后所述涂层中的溶剂基本挥发出去。According to an embodiment of the present invention, the raw materials for preparing the coating further include a solvent, which may be N-methylpyrrolidone (NMP). Typically, the solvent in the coating is substantially volatilized after drying.
根据本发明实施例,所述涂层中含有纳米纤维素、导电剂、粘结剂、分散剂,可选地,纳米纤维素、导电剂、粘结剂、分散剂的质量比为(30-75):(10-40):(1-5):(0.5-3)。According to an embodiment of the present invention, the coating contains nanocellulose, a conductive agent, a binder, and a dispersant. Optionally, the mass ratio of the nanocellulose, a conductive agent, a binder, and a dispersant is (30- 75):(10-40):(1-5):(0.5-3).
本发明还提供上述钠离子二次电池正极集流体的制备方法,包括:The present invention also provides a method for preparing the positive electrode current collector of the above-mentioned sodium ion secondary battery, including:
1)按配比将纳米纤维素、导电剂、粘结剂、分散剂和溶剂混匀,制成固含量为5-50wt%的浆料;1) mixing the nanocellulose, conductive agent, binder, dispersant and solvent according to the proportioning ratio to prepare a slurry with a solid content of 5-50wt%;
2)将所述浆料均匀涂布在金属箔的上下两个表面,干燥;2) The slurry is evenly coated on the upper and lower surfaces of the metal foil, and dried;
3)将步骤2)涂覆后的金属箔在NO2气氛下进行氧化;3) the metal foil coated in step 2) is oxidized under NO atmosphere;
4)将步骤3)氧化后的金属箔热辊压,得到集流体。4) Hot rolling the oxidized metal foil in step 3) to obtain a current collector.
可选地,步骤1)所述浆料的固含量为10-20wt%。若浆料的固含量过低,制造成本高;若浆料的固含量过高,难以均匀分散各物质。Optionally, the solid content of the slurry in step 1) is 10-20wt%. If the solid content of the slurry is too low, the manufacturing cost will be high; if the solid content of the slurry is too high, it will be difficult to uniformly disperse various substances.
可选地,步骤1)在鸿运DL-500L设备中进行充分分散,分散盘线速度10-200m/min,优选60-100m/min,过低难以充分分散;过高,容易打碎分散物质;分散时间120-240min。Optionally, step 1) fully disperse in the Hongyun DL-500L equipment, the linear velocity of the dispersing disc is 10-200m/min, preferably 60-100m/min, if it is too low, it is difficult to fully disperse; if it is too high, it is easy to break the dispersed material; Dispersion time 120-240min.
可选地,步骤2)在科晶智达科技MG200微凹版式涂布机上进行涂布。可选地,涂布走带速度2-10m/min,干燥温度在80-130℃。可选地,干燥后涂层厚度为0.5-5μm,进一步可选为1-2μm。Optionally, step 2) is coated on a Kejing Zhida Technology MG200 micro-gravure coater. Optionally, the coating speed is 2-10m/min, and the drying temperature is 80-130°C. Optionally, the coating thickness after drying is 0.5-5 μm, further optionally 1-2 μm.
可选地,步骤3)NO2流量为10L-30L/min,氧化温度60-120℃。研究发现,高温有利于氧化反应的进行。氧化可以消除纳米纤维素材料中的羟基,防止其在电池充电后与高氧化态的正极材料发生化学反应。Optionally, in step 3) the NO 2 flow rate is 10L-30L/min, and the oxidation temperature is 60-120°C. Studies have found that high temperature is conducive to the oxidation reaction. Oxidation can eliminate the hydroxyl groups in the nanocellulose material, preventing it from chemically reacting with the highly oxidized cathode material after the battery is charged.
可选地,步骤4)热辊压的压力为0.1-2MPa,热辊压的温度在60-80℃。热辊压有利于增强涂层与金属箔之间的结合力。Optionally, the pressure of step 4) hot rolling is 0.1-2 MPa, and the temperature of hot rolling is 60-80°C. Hot rolling is beneficial to enhance the bonding force between the coating and the metal foil.
在一些具体实例,所述钠离子二次电池正极集流体的制备方法包括:In some specific examples, the preparation method of the positive electrode current collector of the sodium ion secondary battery includes:
1)按配比将纳米纤维素、导电剂、粘结剂、分散剂和溶剂在鸿运DL-500L设备中进行充分分散,制成固含量为5-50wt%的浆料;分散盘线速度10-200m/min,优选60-100m/min,分散时间120-240min;1) Fully disperse nanocellulose, conductive agent, binder, dispersant and solvent in Hongyun DL-500L equipment according to the ratio to make a slurry with a solid content of 5-50wt%; the linear speed of the dispersion disc is 10- 200m/min, preferably 60-100m/min, dispersion time 120-240min;
2)将所述浆料在科晶智达科技MG200微凹版式涂布机上均匀涂布于金属箔上下两个表面,涂布走带速度2-10m/min,干燥温度在80-130℃;干燥后涂层厚度在0.5-5μm,优选1-2μm;2) The slurry is evenly coated on the upper and lower surfaces of the metal foil on the Kejing Zhida Technology MG200 micro-gravure coating machine, the coating speed is 2-10m/min, and the drying temperature is 80-130°C; The thickness of the back coating is 0.5-5 μm, preferably 1-2 μm;
3)将步骤2)涂覆后的金属箔在NO2气氛下进行氧化;NO2流量10L-30L/min,氧化温度60-120℃;3) Oxidize the metal foil coated in step 2) under NO 2 atmosphere; NO 2 flow rate 10L-30L/min, oxidation temperature 60-120°C;
4)将步骤3)氧化后的金属箔热辊压,得到集流体;热辊压的压力为0.1-2MPa,热辊压的温度在60-80℃。4) hot-rolling the oxidized metal foil in step 3) to obtain a current collector; the pressure of the hot-rolling is 0.1-2 MPa, and the temperature of the hot-rolling is 60-80°C.
为更好地制备上述钠离子二次电池正极集流体,本发明还提供一种设备,包括依次连接的放卷轴;转移轴;第一微凹版涂布机;第一烘箱;第二微凹版涂布机;第二烘箱;NO2氧化设备;热压辊;收卷轴。其中,NO2氧化设备设有NO2出气口,NO2进气口。In order to better prepare the positive electrode current collector of the above-mentioned sodium ion secondary battery, the present invention also provides a kind of equipment, including the unwinding shaft connected in sequence; the transfer shaft; the first micro-gravure coating machine; the first oven; the second micro-gravure coating Cloth machine; second oven; NO 2 oxidation equipment; hot pressing roller; winding shaft. Among them, NO 2 oxidation equipment is provided with NO 2 outlet and NO 2 inlet.
本发明还包括上述方法制备的钠离子二次电池正极集流体。The present invention also includes the positive current collector of the sodium ion secondary battery prepared by the above method.
本发明还包括上述钠离子二次电池正极集流体在制备钠离子二次电池中的应用。The present invention also includes the application of the above-mentioned positive electrode current collector of the sodium ion secondary battery in the preparation of the sodium ion secondary battery.
本发明还提供一种钠离子二次电池正极极片,包括上述钠离子二次电池正极集流体。在一些实例,还包括涂覆在所述正极集流体上的正极浆料。可选地,所述正极浆料包括NaFe1/3Ni1/3Mn1/3O3、磷酸钒钠、氟磷酸钒钠、普鲁士白等中的一种或几种。The present invention also provides a positive pole piece of a sodium ion secondary battery, comprising the above-mentioned positive current collector of the sodium ion secondary battery. In some examples, a positive electrode slurry coated on the positive electrode current collector is also included. Optionally, the positive electrode slurry includes one or more of NaFe 1/3 Ni 1/3 Mn 1/3 O 3 , sodium vanadium phosphate, sodium vanadium fluorophosphate, Prussian white, and the like.
本发明还提供钠离子二次电池,包括上述钠离子二次电池正极极片;或者包括上述钠离子二次电池正极集流体。The present invention also provides a sodium-ion secondary battery, comprising the above-mentioned positive pole piece of the sodium-ion secondary battery; or comprising the above-mentioned positive current collector of the sodium-ion secondary battery.
本发明涂层中的纳米纤维素隔绝了正极材料与铝箔之间的接触,阻止了两者之间化学反应的发生;与使用传统铝箔作为正极集流体的钠离子二次电池相比,采用本发明制备的钠离子二次电池正极极片压实密度提高了0.1-0.3g/cm3,制成的钠离子电池容量提高20-30%,循环寿命提高70-110%。The nanocellulose in the coating of the present invention isolates the contact between the positive electrode material and the aluminum foil, preventing the chemical reaction between the two; compared with the sodium ion secondary battery using the traditional aluminum foil as the positive electrode current collector, the present invention The compacted density of the cathode sheet of the sodium-ion secondary battery prepared by the invention is increased by 0.1-0.3g/cm3, the capacity of the prepared sodium-ion battery is increased by 20-30%, and the cycle life is increased by 70-110%.
附图说明Description of drawings
图1本发明实施例钠离子二次电池正极集流体示意图。Fig. 1 is a schematic diagram of a positive current collector of a sodium ion secondary battery according to an embodiment of the present invention.
图2本发明实施例制备钠离子二次电池正极集流体的设备示意图。Fig. 2 is a schematic diagram of equipment for preparing a positive electrode collector for a sodium ion secondary battery according to an embodiment of the present invention.
具体实施方式Detailed ways
以下实施例用于说明本发明,但不用来限制本发明的范围。实施例中未注明具体技术或条件者,按照本领域内的文献所描述的技术或条件,或者按照产品说明书进行。所用试剂或仪器未注明生产厂商者,均为可通过正规渠道商购买得到的常规产品。The following examples are used to illustrate the present invention, but are not intended to limit the scope of the present invention. If no specific technique or condition is indicated in the examples, it shall be carried out according to the technique or condition described in the literature in this field, or according to the product specification. The reagents or instruments used were not indicated by the manufacturer, and they were all conventional products that can be purchased through formal channels.
需要说明的是,术语“第一”、“第二”等仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”等的特征可以明示或者隐含地包括一个或者更多个该特征。进一步地,在本发明的描述中,除非另有说明,“多个”的含义是两个或两个以上。It should be noted that terms such as "first" and "second" are used for descriptive purposes only, and should not be understood as indicating or implying relative importance or implicitly indicating the quantity of indicated technical features. Thus, a feature defined as "first", "second", etc. may expressly or implicitly include one or more of that feature. Further, in the description of the present invention, unless otherwise specified, "plurality" means two or more.
如图1所示,本发明实施例提供一种钠离子二次电池正极集流体,包括中间层金属箔2,和分别位于所述中间层两侧的涂层1和3;所述涂层含有纳米纤维素和导电剂。As shown in Fig. 1, the embodiment of the present invention provides a kind of positive electrode current collector of sodium ion secondary battery, comprises middle
如图2所示,本发明实施例提供一种制备钠离子二次电池正极集流体的设备,包括依次连接的放卷轴1;转移轴2;第一微凹版涂布机3;第一烘箱4;第二微凹版涂布机5;第二烘箱6;NO2氧化设备7;热压辊10;收卷轴11。其中,NO2氧化设备7设有NO2出气口8,NO2进气口9。As shown in Figure 2, the embodiment of the present invention provides a kind of equipment that prepares the positive current collector of sodium ion secondary battery, comprises unwinding
如图2所示,所述设备的工作过程如下:铝箔在放卷轴1经过放卷处理;经过转移轴2送至第一微凹版涂布机3,在铝箔上表面涂布浆料(纤维素浆料)并被第一烘箱4烘干;随后进入第二微凹版涂布机5,在铝箔下表面涂布浆料(纤维素浆料),并被第二烘箱6烘干;随后在NO2氧化设备7中对纤维素进行氧化处理;随后在热压辊处10进行碾压处理;在收卷轴11处收卷。As shown in Figure 2, the working process of the device is as follows: the aluminum foil is unwinded on the unwinding
在一些实施例,所涂布的浆料可以由以下实施例制备,也可采用现有技术制备的浆料。In some embodiments, the coated slurry can be prepared from the following examples, or the slurry prepared by the prior art can also be used.
以下钠离子二次电池正极集流体可采用图2所示的设备进行制备。The following cathode current collectors for sodium ion secondary batteries can be prepared using the equipment shown in FIG. 2 .
实施例1Example 1
本实施例提供一种钠离子二次电池正极集流体,制备方法如下:This embodiment provides a current collector for the positive electrode of a sodium ion secondary battery, and the preparation method is as follows:
1)纳米纤维素、导电剂、粘结剂、分散剂按质量比72:25:2:1比例加入NMP中,在鸿运DL-500L设备中进行充分分散制取固含量在10%浆料;分散盘线速度75m/min,分散时间180min;1) Nanocellulose, conductive agent, binder, and dispersant are added to NMP in a mass ratio of 72:25:2:1, and fully dispersed in Hongyun DL-500L equipment to prepare a slurry with a solid content of 10%; The linear speed of the dispersing disc is 75m/min, and the dispersing time is 180min;
纳米纤维素是纤维素纳米晶体直径15-20nm,长度35-45nm;导电剂是乙炔黑,粒径分布在35-45nm;粘结剂是PVDF,分子量在100万;分散剂是PVP,分子量在80万;Nanocellulose is cellulose nanocrystals with a diameter of 15-20nm and a length of 35-45nm; the conductive agent is acetylene black with a particle size distribution of 35-45nm; the binder is PVDF with a molecular weight of 1 million; the dispersant is PVP with a molecular weight of 800 000;
2)上述浆料在科晶智达科技MG200微凹版式涂布机上均匀涂布于15μm厚铝箔上下两个表面,涂布走带速度3m/min,干燥温度在110℃;干燥后涂层厚度在1μm;2) The above slurry is evenly coated on the upper and lower surfaces of 15μm thick aluminum foil on the Kejing Zhida Technology MG200 micro-gravure coating machine, the coating speed is 3m/min, and the drying temperature is 110°C; the coating thickness after drying is 1μm;
3)步骤2)涂覆后的集流体在NO2气氛下进行氧化,NO2流量15L/min;氧化温度100℃;3) Step 2) The coated current collector is oxidized under NO 2 atmosphere, the NO 2 flow rate is 15L/min; the oxidation temperature is 100°C;
4)步骤3)氧化后的集流体在一定的压力下进行热辊压,压力为0.25MPa,热辊压温度在80℃。4) The oxidized current collector in step 3) is hot-rolled under a certain pressure, the pressure is 0.25MPa, and the hot-rolling temperature is 80°C.
实施例2Example 2
本实施例提供一种钠离子二次电池正极集流体,制备方法如下:This embodiment provides a current collector for the positive electrode of a sodium ion secondary battery, and the preparation method is as follows:
1)纳米纤维素、导电剂、粘结剂、分散剂按质量比72:25:2:1比例加入NMP中,在鸿运DL-500L设备中进行充分分散制取固含量在10%浆料;分散盘线速度75m/min,分散时间180min;1) Nanocellulose, conductive agent, binder, and dispersant are added to NMP in a mass ratio of 72:25:2:1, and fully dispersed in Hongyun DL-500L equipment to prepare a slurry with a solid content of 10%; The linear speed of the dispersing disc is 75m/min, and the dispersing time is 180min;
纳米纤维素是与纤维素纳米纤丝的混合物,二者质量比为1:1;纤维素纳米晶体直径15-20nm,长度35-45nm;纤维素纳米纤丝直径5-10nm,长度500-650nm;Nanocellulose is a mixture of cellulose nanofibrils, the mass ratio of the two is 1:1; cellulose nanocrystals have a diameter of 15-20nm and a length of 35-45nm; cellulose nanofibrils have a diameter of 5-10nm and a length of 500-650nm ;
导电剂是乙炔黑与碳纳米管两种混合,乙炔黑与碳纳米管的质量之比为1:1;乙炔黑粒径分布在35-45nm;碳纳米管直径5-10mm,长度50-80nm;粘结剂是PVDF,分子量在100万;分散剂是PVP,分子量在80万;The conductive agent is a mixture of acetylene black and carbon nanotubes, the mass ratio of acetylene black to carbon nanotubes is 1:1; the particle size distribution of acetylene black is 35-45nm; the diameter of carbon nanotubes is 5-10mm, and the length is 50-80nm ;The binder is PVDF with a molecular weight of 1 million; the dispersant is PVP with a molecular weight of 800,000;
2)上述浆料在科晶智达科技MG200微凹版式涂布机上均匀涂布于15μm厚铝箔上下两个表面,涂布走带速度3m/min,干燥温度在110℃;干燥后涂层厚度在1μm;2) The above slurry is evenly coated on the upper and lower surfaces of 15μm thick aluminum foil on the Kejing Zhida Technology MG200 micro-gravure coating machine, the coating speed is 3m/min, and the drying temperature is 110°C; the coating thickness after drying is 1μm;
3)步骤2)涂覆后的集流体在NO2气氛下进行氧化,NO2流量15L/min;氧化温度100℃;3) Step 2) The coated current collector is oxidized under NO 2 atmosphere, the NO 2 flow rate is 15L/min; the oxidation temperature is 100°C;
4)步骤3)氧化后的集流体在一定的压力下进行热辊压,压力为0.25MPa,热辊压温度在80℃。4) The oxidized current collector in step 3) is hot-rolled under a certain pressure, the pressure is 0.25MPa, and the hot-rolling temperature is 80°C.
实施例3Example 3
本实施例提供一种钠离子二次电池正极集流体,制备方法如下:This embodiment provides a current collector for the positive electrode of a sodium ion secondary battery, and the preparation method is as follows:
1)纳米纤维素、导电剂、粘结剂、分散剂按质量比60:37:2:1比例加入NMP中,在鸿运DL-500L设备中进行充分分散制取固含量在10%浆料;分散盘线速度75m/min,分散时间180min;1) Nanocellulose, conductive agent, binder, and dispersant are added to NMP in a mass ratio of 60:37:2:1, and fully dispersed in Hongyun DL-500L equipment to prepare a slurry with a solid content of 10%; The linear speed of the dispersing disc is 75m/min, and the dispersing time is 180min;
纳米纤维素是与纤维素纳米纤丝的混合物,二者质量比为1:1;纤维素纳米晶体直径15-20nm,长度35-45nm;纤维素纳米纤丝直径5-10nm,长度500-650nm;导电剂是乙炔黑与碳纳米管两种混合,乙炔黑与碳纳米管的质量之比为1:1;乙炔黑粒径分布在35-45nm;碳纳米管直径5-10mm,长度50-80nm;粘结剂是PVDF,分子量在100万;分散剂是PVP,分子量在80万;Nanocellulose is a mixture of cellulose nanofibrils, the mass ratio of the two is 1:1; cellulose nanocrystals have a diameter of 15-20nm and a length of 35-45nm; cellulose nanofibrils have a diameter of 5-10nm and a length of 500-650nm The conductive agent is a mixture of acetylene black and carbon nanotubes, the mass ratio of acetylene black to carbon nanotubes is 1:1; the particle size distribution of acetylene black is 35-45nm; the diameter of carbon nanotubes is 5-10mm, and the length is 50- 80nm; the binder is PVDF with a molecular weight of 1 million; the dispersant is PVP with a molecular weight of 800,000;
2)上述浆料在科晶智达科技MG200微凹版式涂布机上均匀涂布于15μm厚铝箔上下两个表面,涂布走带速度3m/min,干燥温度在110℃;干燥后涂层厚度在1μm;2) The above slurry is evenly coated on the upper and lower surfaces of 15μm thick aluminum foil on the Kejing Zhida Technology MG200 micro-gravure coating machine, the coating speed is 3m/min, and the drying temperature is 110°C; the coating thickness after drying is 1μm;
3)步骤2)涂覆后的集流体在NO2气氛下进行氧化,NO2流量15L/min;氧化温度100℃;3) Step 2) The coated current collector is oxidized under NO 2 atmosphere, the NO 2 flow rate is 15L/min; the oxidation temperature is 100°C;
4)步骤3)氧化后的集流体在一定的压力下进行热辊压,压力为0.25MPa,热辊压温度在80℃。4) The oxidized current collector in step 3) is hot-rolled under a certain pressure, the pressure is 0.25MPa, and the hot-rolling temperature is 80°C.
对比例1Comparative example 1
钠离子二次电池正极集流体,与实施例1的区别仅在于,纳米纤维素、导电剂、粘结剂、分散剂的质量比是92:5:2:1。The positive current collector of the sodium ion secondary battery differs from that of Example 1 only in that the mass ratio of nanocellulose, conductive agent, binder, and dispersant is 92:5:2:1.
对比例2Comparative example 2
钠离子二次电池正极集流体,与实施例1的区别仅在于,纳米纤维素、导电剂、粘结剂、分散剂的质量比是10:87:2:1。The positive electrode current collector of the sodium ion secondary battery differs from Example 1 only in that the mass ratio of nanocellulose, conductive agent, binder, and dispersant is 10:87:2:1.
实验例Experimental example
将NaFe1/3Ni1/3Mn1/3O3正极浆料分别涂覆在实施例1-3、对比例1-2制备的钠离子二次电池用集流体,以及市场上购买的普通铝箔(广州纳诺新材料技术有限公司1060铝箔,厚度15μm)上,95℃下烘干,辊压后得到正极极片,进一步分切、卷绕后得到的26650圆柱钠离子二次电池。以质量分数计,正极极片的配比为:NaFe1/3Ni1/3Mn1/3O3 94%,Super P 3%,PVDF3%。The NaFe 1/3 Ni 1/3 Mn 1/3 O 3 cathode slurry is respectively coated on the current collectors for sodium ion secondary batteries prepared in Example 1-3 and Comparative Example 1-2, and the common Aluminum foil (Guangzhou Nano New Material Technology Co., Ltd. 1060 aluminum foil, thickness 15 μm), dried at 95 ° C, rolled to obtain positive pole pieces, further cut and wound to obtain 26650 cylindrical sodium ion secondary batteries. In terms of mass fraction, the proportion of the positive pole piece is: NaFe 1/3 Ni 1/3 Mn 1/3 O 3 94%,
其中,极片最大压实密度测试方法:将涂布后极片裁剪成200×200mm大小,辊压机压力设置为30-60吨,进行辊压,辊压后极片对折,对折有缝隙但不断裂对应的极片压实,即为极片最大压实。Among them, the test method for the maximum compaction density of the pole piece: cut the coated pole piece into a size of 200×200mm, set the pressure of the roller press to 30-60 tons, and perform rolling. After rolling, the pole piece is folded in half. The pole piece corresponding to no fracture is compacted, which is the maximum compaction of the pole piece.
极片阻抗测试方法:将辊压后的极片剪切成4cm×8cm的方形尺寸,把剪切好的极片置于BER2200测试仪探头之间,施加5MPa压力,读取数值。Electrode impedance test method: Cut the rolled electrode into a square size of 4cm×8cm, place the cut electrode between the probes of the BER2200 tester, apply a pressure of 5MPa, and read the value.
电池内阻测试方法:使用RJ3563内阻测定仪在1000Hz条件下测试电池内阻。Battery internal resistance test method: Use the RJ3563 internal resistance tester to test the internal resistance of the battery under the condition of 1000Hz.
对所制得的电池,每个方案取出五个电池在25℃进行循环测试,循环N次,记录第N次与第1次电池放电容量,计算放电保持率。放电保持率=第N次放电容量/第1次放电容量×100%,当循环放电保持率为80%终止循环测试,记录循环次数。测试结果见表1。For the prepared batteries, five batteries were taken out for each scheme to carry out cycle tests at 25°C for N cycles, and the discharge capacities of the N and 1 cells were recorded, and the discharge retention rate was calculated. Discharge retention rate = Nth discharge capacity/1st discharge capacity × 100%, when the cycle discharge retention rate is 80%, the cycle test is terminated, and the number of cycles is recorded. The test results are shown in Table 1.
表1性能测试结果Table 1 performance test results
从上表中可以看出,采用本发明集流体制备的钠离子二次电池相比使用传统铝箔制备的钠离子二次电池,正极极片最大压实密度、电池容量与循环寿命均得到了大幅提高;采用复合纳米纤维素方案的电池在极片最大压实密度、电池容量与循环寿命略优于单一纳米纤维素的电池;提高集流体涂层中导电剂含量,可以继续提高电池的循环寿命。As can be seen from the above table, compared with the sodium ion secondary battery prepared by using the traditional aluminum foil, the maximum compaction density of the positive pole piece, the battery capacity and the cycle life of the sodium ion secondary battery prepared by the current collector of the present invention have been significantly improved. Improvement; the maximum compaction density, battery capacity and cycle life of the battery using the composite nanocellulose solution are slightly better than those of a single nanocellulose battery; increasing the conductive agent content in the current collector coating can continue to improve the cycle life of the battery .
从实施例1与对比例1可以看出,聚丙烯腈过多的加入,极片最大压实密度增大,但是因为导电性变差,电池容量降低,循环寿命变差;从实施例1与对比例2可以看出,聚丙烯腈过少的加入,极片最大压实密度减小,耐碱性变差,导致极片阻抗变大,电池容量降低,循环寿命变差。As can be seen from Example 1 and Comparative Example 1, the addition of too much polyacrylonitrile increases the maximum compacted density of the pole piece, but because of the poor conductivity, the battery capacity decreases and the cycle life deteriorates; from Example 1 and Comparative Example 1 From comparative example 2, it can be seen that too little polyacrylonitrile is added, the maximum compacted density of the pole piece decreases, and the alkali resistance deteriorates, resulting in an increase in the impedance of the pole piece, a decrease in battery capacity, and a poor cycle life.
虽然,上文中已经用一般性说明及具体实施方案对本发明作了详尽的描述,但在本发明基础上,可以对之作一些修改或改进,这对本领域技术人员而言是显而易见的。因此,在不偏离本发明精神的基础上所做的这些修改或改进,均属于本发明要求保护的范围。Although the present invention has been described in detail with general descriptions and specific embodiments above, it is obvious to those skilled in the art that some modifications or improvements can be made on the basis of the present invention. Therefore, the modifications or improvements made on the basis of not departing from the spirit of the present invention all belong to the protection scope of the present invention.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211612519.6A CN116169301B (en) | 2022-12-14 | 2022-12-14 | Current collector for sodium-ion secondary batteries and its preparation method and equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211612519.6A CN116169301B (en) | 2022-12-14 | 2022-12-14 | Current collector for sodium-ion secondary batteries and its preparation method and equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN116169301A true CN116169301A (en) | 2023-05-26 |
| CN116169301B CN116169301B (en) | 2025-12-02 |
Family
ID=86413991
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202211612519.6A Active CN116169301B (en) | 2022-12-14 | 2022-12-14 | Current collector for sodium-ion secondary batteries and its preparation method and equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN116169301B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20160099483A1 (en) * | 2014-10-02 | 2016-04-07 | Lg Chem, Ltd. | Electrode having a dual layer structure, method for manufacturing thereof, and lithium secondary battery comprising the same |
| CN110050369A (en) * | 2016-12-06 | 2019-07-23 | 大韩民国(山林厅国立山林科学院长) | Papery collector, its manufacturing method and the electrochemical appliance comprising papery collector |
| CN111430722A (en) * | 2020-04-07 | 2020-07-17 | 武汉兰钧新能源科技有限公司 | Paper current collector, preparation method thereof, electrode and battery |
| US20210296653A1 (en) * | 2020-03-23 | 2021-09-23 | Kabushiki Kaisha Toshiba | Electrode, secondary battery, battery pack, and vehicle |
| CN114695840A (en) * | 2022-03-30 | 2022-07-01 | 大连中比动力电池有限公司 | A kind of sodium ion battery positive electrode sheet, sodium ion battery and preparation method and system thereof |
-
2022
- 2022-12-14 CN CN202211612519.6A patent/CN116169301B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20160099483A1 (en) * | 2014-10-02 | 2016-04-07 | Lg Chem, Ltd. | Electrode having a dual layer structure, method for manufacturing thereof, and lithium secondary battery comprising the same |
| CN110050369A (en) * | 2016-12-06 | 2019-07-23 | 大韩民国(山林厅国立山林科学院长) | Papery collector, its manufacturing method and the electrochemical appliance comprising papery collector |
| US20210296653A1 (en) * | 2020-03-23 | 2021-09-23 | Kabushiki Kaisha Toshiba | Electrode, secondary battery, battery pack, and vehicle |
| CN111430722A (en) * | 2020-04-07 | 2020-07-17 | 武汉兰钧新能源科技有限公司 | Paper current collector, preparation method thereof, electrode and battery |
| CN114695840A (en) * | 2022-03-30 | 2022-07-01 | 大连中比动力电池有限公司 | A kind of sodium ion battery positive electrode sheet, sodium ion battery and preparation method and system thereof |
Non-Patent Citations (1)
| Title |
|---|
| 胡雨萌;侯敏杰;许苗军;李斌;: "纤维素基一体化三明治结构超级电容器的制备及性能", 林产化学与工业, no. 03, 28 June 2020 (2020-06-28) * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN116169301B (en) | 2025-12-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108306013B (en) | Fast-charging and fast-discharging type high-power lithium ion battery and manufacturing method thereof | |
| CN107978732B (en) | Pole piece and battery | |
| CN111540880B (en) | Negative plate, preparation method and lithium ion battery comprising negative plate | |
| CN102208598A (en) | Electrode plate of graphene coating modified lithium secondary battery and manufacturing method thereof | |
| CN111900360B (en) | Quick-charging type high-specific-capacity negative plate and lithium ion battery comprising same | |
| CN105958008A (en) | Composite positive electrode plate of lithium ion battery, preparation method thereof and lithium ion battery | |
| CN105489392B (en) | A kind of graphene pole piece and preparation method thereof | |
| CN114156602B (en) | Solid electrolyte membrane with multiple coatings, preparation method and application | |
| CN115621412A (en) | Lithium ion battery positive plate, preparation method and lithium ion battery | |
| WO2022057666A1 (en) | Positive electrode sheet and battery | |
| KR20210124887A (en) | Pre-lithiated negative electrode, manufacturing method thereof, and lithium ion battery and supercapacitor comprising pre-lithiated negative electrode | |
| CN116387509A (en) | Composite positive electrode for lithium metal battery and preparation method thereof | |
| CN111799437A (en) | Positive pole piece and sodium ion battery | |
| CN109037592A (en) | Lithium ion battery positive plate, preparation method thereof and lithium ion battery | |
| CN108987671A (en) | A kind of high safety anode composite pole piece, preparation method and its application | |
| CN112467308A (en) | Diaphragm, preparation method thereof and lithium ion battery | |
| CN116885182A (en) | Dry electrode film, preparation method and application thereof | |
| CN115425210A (en) | Binary high-nickel sodium-ion battery positive electrode material, preparation method and application | |
| WO2025044577A1 (en) | Graphite negative electrode material and preparation method therefor, and battery | |
| CN114927642B (en) | Negative plate, preparation method and lithium ion battery | |
| CN117334836A (en) | A kind of positive electrode sheet and battery | |
| CN116780097A (en) | Porous functional coating diaphragm, preparation method thereof and lithium ion battery | |
| CN110518224A (en) | A kind of preparation method of lithium ion battery carbon silicon anode material | |
| CN115000343A (en) | Preparation method of flexible double-layer self-supporting electrode | |
| CN119092644A (en) | A lithium ion multilayer electrode and its preparation method and application |
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 | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20231127 Address after: 211399 Factory Building No. 6, Phase II, Standard Factory Building, No. 86 Shuanggao Road, Economic Development Zone, Gaochun District, Nanjing City, Jiangsu Province Applicant after: Nanjing Bifeida New Energy Technology Co.,Ltd. Address before: 116450 No. 11, East Rose Street, Huayuankou Economic Zone, Dalian City, Liaoning Province Applicant before: DALIAN CBAK POWER BATTERY CO.,LTD. |
|
| TA01 | Transfer of patent application right | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |