CN105648422A - Gaseous phase atomic layer deposition device for electrode powder material coating and application - Google Patents
Gaseous phase atomic layer deposition device for electrode powder material coating and application Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45523—Pulsed gas flow or change of composition over time
- C23C16/45525—Atomic layer deposition [ALD]
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/362—Composites
- H01M4/366—Composites as layered products
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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Abstract
Description
技术领域technical field
本申请涉及锂离子电池的电极材料加工领域,特别是涉及一种用于锂离子电池的电极粉体材料包覆的气相原子层沉积装置及其应用。The present application relates to the field of electrode material processing for lithium-ion batteries, in particular to a gas-phase atomic layer deposition device for covering electrode powder materials of lithium-ion batteries and its application.
背景技术Background technique
锂离子电池因其具有高比容量、高循环性能、高能量密度以及高功率密度等优良的性能,已经广泛应用于小型移动数码电子产品,包括手机、相机、笔记本电脑等。随着锂离子电池技术的迅猛发展,锂离子电池也被公认为是最具有发展前景的电动汽车动力储能电池。锂离子电池的电极粉体材料,其性能在很大程度上决定着锂离子电池的性能。研究显示,通过在电极粉体材料包覆改性能够有效提高锂离子电池的性能。Lithium-ion batteries have been widely used in small mobile digital electronic products, including mobile phones, cameras, and notebook computers, due to their excellent performance such as high specific capacity, high cycle performance, high energy density, and high power density. With the rapid development of lithium-ion battery technology, lithium-ion batteries are also recognized as the most promising power storage batteries for electric vehicles. The performance of electrode powder materials for lithium-ion batteries largely determines the performance of lithium-ion batteries. Studies have shown that the performance of lithium-ion batteries can be effectively improved by coating and modifying electrode powder materials.
现有的锂离子电池的电极粉体材料包覆方法主要有固相法、液相法和气相法。其中,原子层沉积技术是一种特殊的化学气相沉积技术,制备的膜层具有均匀、致密、厚度精确可控、高保形性等优点。利用原子层沉积技术进行电极粉体材料包覆,是指在电极粉体材料表面通过自限制化学吸附反应,得到一层非常均匀的纳米级厚度的膜层。The existing coating methods of electrode powder materials for lithium-ion batteries mainly include solid-phase method, liquid-phase method and gas-phase method. Among them, atomic layer deposition technology is a special chemical vapor deposition technology, and the prepared film has the advantages of uniformity, compactness, precise and controllable thickness, and high conformality. The use of atomic layer deposition technology to coat electrode powder materials refers to obtaining a very uniform nanometer-thick film layer on the surface of electrode powder materials through self-limiting chemical adsorption reactions.
但是,锂离子电池的电极粉体材料具有较大的比表面积和较高的比表面能,这导致严重的颗粒团聚现象,影响包覆的均匀性和效率,进而影响包覆改性电极粉体材料的性能以及锂离子电池的性能。这在进行工业化生产的大量粉体包覆时尤为严重;严重制约了锂离子电池电极粉体材料包覆改性的进一步发展以及大规模的工业化应用。因此,有必要对传统的对基片表面进行原子层沉积的装置进行改进,以满足锂离子电池电极粉体材料这种特殊粉体材料包覆改性的生产需求。However, the electrode powder materials of lithium-ion batteries have a large specific surface area and high specific surface energy, which leads to serious particle agglomeration, affects the uniformity and efficiency of coating, and then affects the coating modified electrode powder. The properties of materials and the performance of lithium-ion batteries. This is especially serious when a large amount of powder coating is carried out in industrial production; it seriously restricts the further development of coating modification of lithium ion battery electrode powder materials and large-scale industrial application. Therefore, it is necessary to improve the traditional device for atomic layer deposition on the surface of the substrate to meet the production requirements of coating modification of special powder materials such as lithium-ion battery electrode powder materials.
发明内容Contents of the invention
本申请的目的是提供一种改进的特别用于锂离子电池的电极粉体材料包覆的气相原子层沉积装置及其应用。The purpose of this application is to provide an improved vapor phase atomic layer deposition device and its application, which are especially used for electrode powder material coating of lithium ion batteries.
本申请采用了以下技术方案:The application adopts the following technical solutions:
本申请的一方面公开了一种用于电极粉体材料包覆的气相原子层沉积装置,包括真空反应腔体和监控系统,真空反应腔体中设置有搅拌装置,搅拌装置与监控系统电连接或信号连接,通过监控系统控制搅拌装置运行。One aspect of the present application discloses a vapor phase atomic layer deposition device for electrode powder material coating, including a vacuum reaction chamber and a monitoring system, a stirring device is arranged in the vacuum reaction chamber, and the stirring device is electrically connected to the monitoring system Or signal connection, control the operation of the stirring device through the monitoring system.
本申请的气相原子层沉积装置,是一种实现气固交替反应的装置,具体的,是在反应腔体中放入固体颗粒,然后通入气相前驱体,气相前驱体与固体颗粒接触,在固体颗粒表面吸附、反应,形成包覆层的装置。因为气相前驱体是分子或原子形式在固体颗粒表面进行吸附、反应,以单原子膜形式一层一层的包覆在固体颗粒表面的,所以称为气相原子层沉积。The gas-phase atomic layer deposition device of the present application is a device that realizes gas-solid alternating reaction. Specifically, solid particles are placed in the reaction chamber, and then the gas-phase precursor is fed into the gas-phase precursor. The gas-phase precursor is in contact with the solid particles. A device that adsorbs and reacts on the surface of solid particles to form a coating. Because gas-phase precursors are adsorbed and reacted on the surface of solid particles in the form of molecules or atoms, and are coated layer by layer on the surface of solid particles in the form of monoatomic films, it is called gas-phase atomic layer deposition.
需要说明的是,本申请的关键在于,以现有的气相原子层沉积装置为基础,在其真空反应腔体中设置搅拌装置,利用搅拌装置将电极粉体材料充分分散,减少电极粉体材料团聚,利于前驱体吸附和反应,从而使得气相原子层沉积更均匀,生产出高质量的电极包覆材料;并且,本申请的气相原子层沉积装置特别适合于大批量电极粉体材料的处理,能够满足工业化大规模生产的需求。此外,搅拌装置跟监控系统的连接,主要是为了便于实时监控和控制搅拌装置的转动速度。本申请的关键在于增加搅拌装置,至于其它的,如真空系统、前驱体系统、加热系统,以及监控系统等,都可以参考现有的气相原子层沉积装置,在此不累述。It should be noted that the key point of this application is that, based on the existing gas-phase atomic layer deposition device, a stirring device is installed in the vacuum reaction chamber, and the electrode powder material is fully dispersed by the stirring device to reduce the amount of electrode powder material. Agglomeration is conducive to the adsorption and reaction of precursors, so that the vapor phase atomic layer deposition is more uniform, and high-quality electrode coating materials are produced; moreover, the vapor phase atomic layer deposition device of the present application is particularly suitable for the processing of large quantities of electrode powder materials, It can meet the needs of industrialized mass production. In addition, the connection between the stirring device and the monitoring system is mainly for the convenience of real-time monitoring and control of the rotation speed of the stirring device. The key to this application is to add a stirring device. As for others, such as vacuum system, precursor system, heating system, and monitoring system, etc., you can refer to the existing vapor phase atomic layer deposition device, and will not repeat it here.
因此,本申请的一种实现方式中,气相原子层沉积装置还包括真空系统、前驱体系统和加热系统;真空系统用于对真空反应腔体抽真空,前驱体系统用于向真空反应腔体提供前驱体,加热系统用于给真空反应腔体加热,监控系统用于检测真空反应腔体内的压力和温度,并控制真空系统、前驱体系统和加热系统的开启或关闭。Therefore, in one implementation of the present application, the vapor phase atomic layer deposition device also includes a vacuum system, a precursor system and a heating system; the vacuum system is used to evacuate the vacuum reaction chamber, and the precursor system is used to pump the vacuum reaction chamber The precursor is provided, the heating system is used to heat the vacuum reaction chamber, and the monitoring system is used to detect the pressure and temperature in the vacuum reaction chamber, and control the opening or closing of the vacuum system, the precursor system and the heating system.
优选的,搅拌装置为桨式搅拌、涡轮式搅拌和框式搅拌中的至少一种。Preferably, the stirring device is at least one of paddle stirring, turbine stirring and frame stirring.
需要说明的是,本申请的搅拌装置,其目的就是将电极粉体材料扬起,使其充分分散,以便于前驱体吸附和反应;因此,只要能够将电极粉体材料扬起即可,至于采用怎样的具体结构可以根据不同的生产条件而定,本申请的优选方案中采用桨式搅拌、涡轮式搅拌和框式搅拌中的至少一种实现搅拌功能。可以理解,在生产条件允许或者一些特殊情况下,甚至可以采用类似洗衣机滚筒转动的结构和方式,使电极粉体材料扬起,例如真空反应腔体自身转动,这种情况下,真空反应腔体自身结构就相当于本申请的搅拌装置。It should be noted that the purpose of the stirring device of the present application is to raise the electrode powder material and make it fully dispersed so as to facilitate the adsorption and reaction of the precursor; therefore, as long as the electrode powder material can be raised, as for The specific structure to be adopted can be determined according to different production conditions. In the preferred solution of the present application, at least one of paddle stirring, turbine stirring and frame stirring is used to realize the stirring function. It can be understood that, when production conditions permit or in some special cases, a structure and method similar to the rotation of a washing machine drum can even be used to raise the electrode powder material, such as the vacuum reaction chamber itself rotating. In this case, the vacuum reaction chamber The structure itself is equivalent to the stirring device of the present application.
优选的,真空反应腔体由上腔体和下腔体组成,搅拌装置的一端固定在上腔体顶端,另一端伸入下腔体中。Preferably, the vacuum reaction chamber is composed of an upper chamber and a lower chamber, one end of the stirring device is fixed on the top of the upper chamber, and the other end extends into the lower chamber.
本申请的另一面公开了本申请的气相原子层沉积装置在粉体材料的表面包覆中的应用。Another aspect of the present application discloses the application of the vapor phase atomic layer deposition device of the present application in the surface coating of powder materials.
需要说明的是,本申请的气相原子层沉积装置虽然是针对电极粉体材料的包覆而设计的,但是,本申请的气相原子层沉积装置并不仅限用于电极粉体材料的包覆,任何需要包覆的颗粒都可以采用本申请的气相原子层沉积装置。It should be noted that although the vapor-phase atomic layer deposition device of the present application is designed for the coating of electrode powder materials, the vapor-phase atomic layer deposition device of the present application is not limited to the coating of electrode powder materials. Any particle that needs to be coated can use the vapor phase atomic layer deposition device of the present application.
本申请的另一面公开了一种电极粉体材料包覆的方法,其中,电极粉体材料为锂离子电池正极粉体材料或锂离子电池负极粉体材料,该方法采用本申请的气相原子层沉积装置对电极粉体材料进行包覆改性。Another aspect of the application discloses a method for coating electrode powder materials, wherein the electrode powder materials are positive electrode powder materials for lithium-ion batteries or negative electrode powder materials for lithium-ion batteries, and the method uses the gas phase atomic layer of the application The deposition device coats and modifies the electrode powder material.
本申请的一种具体实现方式中,该方法包括以下步骤,In a specific implementation of the present application, the method includes the following steps,
(a)将待处理的电极粉体材料装入气相原子层沉积装置的真空反应腔体;(a) loading the electrode powder material to be processed into the vacuum reaction chamber of the vapor phase atomic layer deposition device;
(b)对真空反应腔体进行抽真空,维持真空反应腔体跟外部空气环境的有效隔离;(b) Vacuumize the vacuum reaction chamber to maintain effective isolation between the vacuum reaction chamber and the external air environment;
(c)利用搅拌装置将电极粉体材料扬起,使其充分分散;(c) Use a stirring device to raise the electrode powder material to fully disperse it;
(d)向真空反应腔体中通入第一种气相前驱体,使其吸附在电极粉体材料表面;(d) Passing the first gas phase precursor into the vacuum reaction chamber to make it adsorb on the surface of the electrode powder material;
(e)通入载气将真空反应腔体中多余的第一种气相前驱体清除;(e) feed carrier gas to remove excess first gas phase precursor in the vacuum reaction chamber;
(f)向真空反应腔体中通入第二种气相前驱体,使之与吸附在电极粉体材料表面的第一种气相前驱体反应,形成包覆层;(f) introducing a second gas-phase precursor into the vacuum reaction chamber to react with the first gas-phase precursor adsorbed on the surface of the electrode powder material to form a coating layer;
(g)通入载气将真空反应腔体中多余的第二种气相前驱体清除;(g) feed the carrier gas to remove the redundant second gas phase precursor in the vacuum reaction chamber;
重复步骤(d)至(g)直到获得设定厚度或结构的包覆层。Steps (d) to (g) are repeated until a coating of a defined thickness or structure is obtained.
需要说明的是,步骤(d)至(g)实际上即可完成一层气相原子层沉积包覆,但是,为了获得更厚的包覆层,通常需要进行多次沉积,因此,需要重复步骤(d)至(g)直到获得所需厚度的包覆层;至于具体需要重复多少次,取决于所采用的具体的第一种气相前驱体和第二种气相前驱体,以及具体所需要的包覆层厚度,在此不做具体限定。It should be noted that steps (d) to (g) can actually complete one layer of vapor-phase atomic layer deposition coating, but in order to obtain a thicker coating layer, it is usually necessary to perform multiple depositions, so the steps need to be repeated (d) to (g) until the cladding layer of the desired thickness is obtained; as for how many times it needs to be repeated, it depends on the specific first gas phase precursor and the second gas phase precursor used, and the specific required The thickness of the coating layer is not specifically limited here.
还需要说明的是,采用本申请的气相原子层沉积装置和方法可以对电极粉体材料进行一种、两种,甚至多种材料的包覆,形成不同结构的包覆层,只要改变相应的第一种气相前驱体和第二种气相前驱体即可。此外,第一种气相前驱体和第二种气相前驱体,实际上是假设,两种前驱体反应即可获得包覆层,这是获得包覆层比较常规的反应模式,因此这样假设。It should also be noted that, using the vapor phase atomic layer deposition device and method of the present application, one, two, or even multiple materials can be used to coat the electrode powder materials to form coating layers with different structures, as long as the corresponding The first gas-phase precursor and the second gas-phase precursor are sufficient. In addition, the first gas-phase precursor and the second gas-phase precursor actually assume that the coating layer can be obtained by reacting the two precursors. This is a relatively conventional reaction mode for obtaining the coating layer, so this assumption is made.
可以理解,如果第一种气相前驱体吸附在电极粉体材料表面,然后经过一些特殊条件就可以形成包覆层,当然就不需要再通入第二种气相前驱体,即可以省略步骤(f)和(g)。或者,如果需要更多种气相前驱体才能反应生成包覆层,例如还需要第三种气相前驱体、第四种气相前驱体,甚至更多前驱体的情况下,相应的增加通入气相前驱体、载气清洗多余的气相前驱体,再通入另一种气相前驱体、再进行载气清洗,如此反复即可。It can be understood that if the first gas-phase precursor is adsorbed on the surface of the electrode powder material, and then the coating layer can be formed after some special conditions, of course there is no need to feed the second gas-phase precursor, that is, the step (f ) and (g). Or, if more gas-phase precursors are needed to react to form the cladding layer, for example, a third gas-phase precursor, a fourth gas-phase precursor, or even more precursors are required, correspondingly increase the gas-phase precursor Clean the excess gas-phase precursor with the carrier gas, then pass in another gas-phase precursor, and then clean with the carrier gas, and so on.
优选的,搅拌装置的搅拌速度为100-1000转每分钟。Preferably, the stirring speed of the stirring device is 100-1000 revolutions per minute.
需要说明的是,搅拌速度是根据锂离子电池的电极粉体材料颗粒原始粒径和质量的不同而调节的;转速过低,堆积的电极粉体材料无法充分分散,转速过高,电极粉体材料颗粒由于离心力的作用,会向反应腔体壁靠拢,有悖于电极粉体材料分散的初衷。为此,经过大量的试验证实,对于原始粒径和质量大的微米级颗粒的电极粉体材料,调节搅拌速度500-1000转每分钟,可以达到较理想的粉体分散效果;而对原始粒径和质量小的纳米级颗粒的电极粉体材料,调节搅拌速度100-500转每分钟,可以达到较理想的粉体分散效果。It should be noted that the stirring speed is adjusted according to the original particle size and quality of the electrode powder material particles of the lithium-ion battery; if the speed is too low, the accumulated electrode powder material cannot be fully dispersed; if the speed is too high, the electrode powder Due to the effect of centrifugal force, the material particles will move closer to the wall of the reaction chamber, which is contrary to the original intention of electrode powder material dispersion. For this reason, a large number of experiments have confirmed that for electrode powder materials with primary particle size and mass of micron-sized particles, adjusting the stirring speed at 500-1000 rpm can achieve a more ideal powder dispersion effect; Electrode powder materials with nano-sized particles with small diameter and mass, and adjusting the stirring speed at 100-500 rpm can achieve a more ideal powder dispersion effect.
优选的,真空反应腔体中,第一种气相前驱体与第二种气相前驱体的反应温度为50-300℃。Preferably, in the vacuum reaction chamber, the reaction temperature of the first gas-phase precursor and the second gas-phase precursor is 50-300°C.
需要说明的是,第一种气相前驱体与第二种气相前驱体的反应温度,实际上就是真空反应腔体内的温度,这是由监控系统控制加热系统进行加热,使其保持在所需温度;其中,具体的反应温度是根据所采用的具体的前驱体及其所需的反应温度而定的,在此不做具体限定;通常来说,根据电极粉体材料所采用的包覆材料,反应温度都是在50-300℃之间。It should be noted that the reaction temperature of the first gas-phase precursor and the second gas-phase precursor is actually the temperature in the vacuum reaction chamber, which is controlled by the monitoring system to heat the heating system to keep it at the required temperature ; Wherein, the specific reaction temperature is determined according to the specific precursor used and its required reaction temperature, and is not specifically limited here; generally speaking, according to the coating material used for the electrode powder material, The reaction temperature is all between 50-300°C.
优选的,载气为惰性气体。更优选的,载气为氮气或氩气。Preferably, the carrier gas is an inert gas. More preferably, the carrier gas is nitrogen or argon.
优选的,载气的温度为50-300℃。Preferably, the temperature of the carrier gas is 50-300°C.
需要说明的是,载气的一个主要用途是将第一种气相前驱体和第二种气相前驱体清洗干净,但是,为了避免对真空反应腔体内的温度造成影响,因此,采用温度为50-300℃的载气;可以理解,具体的载气温度是与真空反应腔体中的反应温度一致的,在此不做具体限定。It should be noted that one of the main purposes of the carrier gas is to clean the first gas-phase precursor and the second gas-phase precursor. However, in order to avoid affecting the temperature in the vacuum reaction chamber, a temperature of 50- 300°C carrier gas; it can be understood that the specific carrier gas temperature is consistent with the reaction temperature in the vacuum reaction chamber, and is not specifically limited here.
优选的,第一种气相前驱体和第二种气相前驱体的温度为50-200℃。Preferably, the temperature of the first gas-phase precursor and the second gas-phase precursor is 50-200°C.
需要说明的是,前驱体的熔点越高,其饱和蒸汽压越低,同等条件下获得的可以参与反应的前驱体量就越少;因此,对于普通前驱体,温度控制在50-100摄氏度;对于熔点很高的固态前驱体,温度可以达到200摄氏度。可以理解,为了防止前驱体在输送管路中的冷凝,因此,还需要对管路进行加热,使其温度控制在50-200摄氏度。It should be noted that the higher the melting point of the precursor, the lower its saturated vapor pressure, and the less the amount of precursor that can participate in the reaction obtained under the same conditions; therefore, for common precursors, the temperature is controlled at 50-100 degrees Celsius; For solid precursors with very high melting points, the temperature can reach 200 degrees Celsius. It can be understood that, in order to prevent the precursor from condensing in the delivery pipeline, it is necessary to heat the pipeline so that its temperature is controlled at 50-200 degrees Celsius.
本申请的有益效果在于:The beneficial effect of this application is:
本申请的气相原子层沉积装置,特别针对锂离子电池电极粉体的包覆改性而设计,在反应腔体内增加搅拌装置,利用搅拌装置搅拌锂离子电池的电极粉体材料,并且,通过调节搅拌装置的转速和方向,使不同质量和粒径的电极粉体材料得到充分分散,有效减少粉体的团聚程度,利于前驱体的吸附和反应,提高了包覆均匀性和包覆效率,为工业化大规模生产高质量的锂离子电池电极粉体包覆材料奠定了基础。The gas-phase atomic layer deposition device of the present application is specially designed for the coating and modification of lithium-ion battery electrode powder. A stirring device is added in the reaction chamber, and the stirring device is used to stir the electrode powder material of the lithium-ion battery, and, by adjusting The rotation speed and direction of the stirring device can fully disperse electrode powder materials of different quality and particle size, effectively reduce the degree of powder agglomeration, facilitate the adsorption and reaction of precursors, and improve the coating uniformity and coating efficiency. The industrialized large-scale production of high-quality lithium-ion battery electrode powder coating materials has laid the foundation.
附图说明Description of drawings
图1是本申请实施例中气相原子层沉积装置的结构示意图;Fig. 1 is a schematic structural diagram of a vapor phase atomic layer deposition device in an embodiment of the present application;
图2是本申请实施例中电极粉体材料包覆方法的流程示意框图;Fig. 2 is a schematic block diagram of the process flow of the electrode powder material coating method in the embodiment of the present application;
图3是本申请实施例中电极粉体材料包覆前后的透射电子显微镜图,(a)为包覆前的扫描结果,(b)为包覆后的扫描结果。Fig. 3 is a transmission electron microscope image of the electrode powder material before and after coating in the embodiment of the present application, (a) is the scanning result before coating, and (b) is the scanning result after coating.
具体实施方式detailed description
本申请的气相原子层沉积装置,特别针对锂离子电池电极粉体材料的包覆而改进,具体的,在真空反应腔体中设置搅拌装置,利用搅拌装置将电极粉体材料扬起,使其分散,从而利于前驱体均匀有效的吸附在电极粉体材料颗粒表面,使得气相原子层沉积包覆更均匀。The gas-phase atomic layer deposition device of the present application is especially improved for the coating of lithium-ion battery electrode powder materials. Specifically, a stirring device is installed in the vacuum reaction chamber, and the electrode powder material is raised by the stirring device to make it Dispersion, which facilitates the uniform and effective adsorption of the precursor on the surface of the electrode powder material particles, making the vapor phase atomic layer deposition coating more uniform.
可以理解,本申请的用于电极粉体材料包覆的气相原子层沉积装置,虽然是特别针对锂离子电池电极粉体材料的包覆而改进,但是,该气相原子层沉积装置并不仅限用于锂离子电池电极粉体材料的包覆,也可以用于其他各种需要在颗粒表面形成一层包覆层的情况。It can be understood that although the gas-phase atomic layer deposition device used for electrode powder material coating of the present application is specially improved for the coating of lithium-ion battery electrode powder materials, the gas-phase atomic layer deposition device is not limited to use It can be used for the coating of lithium-ion battery electrode powder materials, and can also be used in various other situations where a coating layer needs to be formed on the particle surface.
需要说明的是,本申请的电极粉体材料包覆的方法,是采用的比较普遍的两种前驱体反应形成包覆层的情况;本申请的气相原子层沉积装置或包覆方法,并不只限于两种前驱体,还可以采用三种或者更多种前驱体按照一定顺序实现多层膜结构的制备,相应的在包覆方法中,于第二种气相前驱体清洗后,通入第三种气相前驱体,然后采用载气清洗第三种气相前驱体,通入第四种气相前驱体、载气清洗,以此类推。It should be noted that the coating method of the electrode powder material in this application is the situation where two precursors react to form a coating layer; the vapor phase atomic layer deposition device or coating method in this application is not only Limited to two precursors, three or more precursors can also be used in a certain order to realize the preparation of multilayer film structures. Correspondingly, in the coating method, after the second gas phase precursor is cleaned, the third One gas-phase precursor, then the third gas-phase precursor is cleaned with carrier gas, the fourth gas-phase precursor is introduced, carrier gas is cleaned, and so on.
此外,在通入前驱体后,可以采用保压吸附或不保压吸附,保压吸附即在通入前驱体时,关闭真空系统,让真空反应腔体内保持一定的气压,以便于前驱体吸附,一段时间后再开启真空系统,将前驱体抽离;不保压吸附,则是在通入前驱体时,开启真空系统,使真空反应腔体内的气压始终保持在初始气压。具体采用保压吸附还是不保压吸附,可以根据各个前驱体的吸附难易程度而定,在此不做具体限定。In addition, after the precursor is introduced, pressure-holding adsorption or non-pressure-holding adsorption can be used. Pressure-holding adsorption means that when the precursor is introduced, the vacuum system is turned off to maintain a certain air pressure in the vacuum reaction chamber to facilitate the adsorption of the precursor. After a period of time, turn on the vacuum system to extract the precursor; without pressure-holding adsorption, the vacuum system is turned on when the precursor is introduced, so that the air pressure in the vacuum reaction chamber is always maintained at the initial air pressure. The specific use of pressure-holding adsorption or no-pressure-holding adsorption can be determined according to the difficulty of adsorption of each precursor, and is not specifically limited here.
下面通过具体实施例对本申请作进一步详细说明。以下实施例仅对本申请进行进一步说明,不应理解为对本申请的限制。The present application will be described in further detail below through specific examples. The following examples only further illustrate the present application, and should not be construed as limiting the present application.
实施例Example
本例的用于电极粉体材料包覆的气相原子层沉积装置,由真空反应腔体、真空系统、前驱体系统、加热系统,以及监控系统组成。其中,前驱体系统用于向真空反应腔体输入载气和气相前驱体。加热系统用于对真空反应腔体、前驱体容器和连接管路加热。真空系统用于维持真空反应腔体的真空、调整真空反应腔体的内部压力以及真空反应腔体内残余前驱体、副产物等的排出。监控系统用于监测并显示真空反应腔体内部的压力、反应区域的温度,真空反应腔体外壁温度、前驱体容器温度、连接管路温度等;并控制前驱体系统中前驱体脉冲时间与流量、循环次数以及载气清洗时间与流量,控制加热系统和真空系统的开关。The vapor phase atomic layer deposition device used for electrode powder material coating in this example consists of a vacuum reaction chamber, a vacuum system, a precursor system, a heating system, and a monitoring system. Among them, the precursor system is used to input carrier gas and gas phase precursor into the vacuum reaction chamber. The heating system is used to heat the vacuum reaction chamber, precursor container and connecting pipelines. The vacuum system is used to maintain the vacuum of the vacuum reaction chamber, adjust the internal pressure of the vacuum reaction chamber, and discharge residual precursors and by-products in the vacuum reaction chamber. The monitoring system is used to monitor and display the pressure inside the vacuum reaction chamber, the temperature of the reaction area, the outer wall temperature of the vacuum reaction chamber, the temperature of the precursor container, the temperature of the connecting pipeline, etc.; and control the pulse time and flow rate of the precursor in the precursor system , cycle times, carrier gas cleaning time and flow rate, control the switch of heating system and vacuum system.
本例中,真空反应腔体如图1所示,整个真空反应腔体依靠在支撑架15上,真空反应腔体由下腔体1和上腔体2组成,下腔体1固定在支撑架15上,上腔体2通过导轨轮14连接在支撑架15上,上腔体2通过导轨轮14可沿支撑架15上下移动;搅拌装置4的一端固定在上腔体2顶端,通过密封件3密封,在上腔体2和下腔体1合拢时,搅拌装置4另一端伸入下腔体1中。另外,真空反应腔体上还开设有填料口5、进气口6、出气口7、下腔体热油进口8、下腔体热油出口9、上腔体热油进口10和上腔体热油出口11。In this example, the vacuum reaction chamber is shown in Figure 1. The entire vacuum reaction chamber rests on the support frame 15. The vacuum reaction chamber is composed of a lower chamber 1 and an upper chamber 2, and the lower chamber 1 is fixed on the support frame. 15, the upper cavity 2 is connected to the support frame 15 through the guide wheel 14, and the upper cavity 2 can move up and down along the support frame 15 through the guide wheel 14; one end of the stirring device 4 is fixed on the top of the upper cavity 2, through the seal 3 sealing, when the upper cavity 2 and the lower cavity 1 are closed, the other end of the stirring device 4 extends into the lower cavity 1. In addition, the vacuum reaction chamber is also provided with a filling port 5, an air inlet 6, an air outlet 7, a lower chamber hot oil inlet 8, a lower chamber hot oil outlet 9, an upper chamber hot oil inlet 10 and an upper chamber hot oil inlet 10. Hot oil outlet 11.
其中,填料口5设置于上腔体2的顶端,用于加入电极体材料。进气口6开设于下腔体1的底端,用于连接前驱体系统;本例中,前驱体系统包括两条并联的前驱体输送支路,分别提供第一种气相前驱体和第二种气相前驱体的前驱体原料,前驱体原料通过进气口6通入真空反应腔体。出气口开设于上腔体2的顶端,位于填料口5旁边,用于连接真空系统,真空系统的真空泵13通过出气口7对真空反应腔体进行抽气,以维持真空反应腔体的真空、调整真空反应腔体内部压力以及真空反应腔体内残余前驱体和/或副产物的排出等;并且,在本申请的一种实现方式中,在真空泵13和出气口7之间还设置有粉尘过滤装置12,用于过滤残余前驱体和/或副产物以及载气从反应腔体带出的少量粉尘。下腔体热油进口8和下腔体热油出口9开设于下腔体1上,下腔体热油进口8开设于下腔体1的下部侧面,下腔体热油出口9开设于下腔体1的上部侧面,用于连接加热系统,加热后的热油经过下腔体热油进口8进入,然后由下腔体热油出口9排出,这个过程中,将热量传递给下腔体1,以实现对下腔体1加热。类似的,开设于上腔体2的上腔体热油进口10和上腔体热油出口11,同样也是用于连接加热系统,通过热油对上腔体2进行加热。Wherein, the filling port 5 is arranged on the top of the upper cavity 2 for adding the material of the electrode body. The air inlet 6 is opened at the bottom of the lower cavity 1, and is used to connect the precursor system; in this example, the precursor system includes two parallel precursor delivery branches, respectively providing the first gas phase precursor and the second The precursor raw material of a gas phase precursor, the precursor raw material is passed into the vacuum reaction chamber through the air inlet 6. The air outlet is opened on the top of the upper chamber 2, next to the filling port 5, and is used to connect the vacuum system. The vacuum pump 13 of the vacuum system pumps air through the air outlet 7 to the vacuum reaction chamber to maintain the vacuum of the vacuum reaction chamber. Adjust the internal pressure of the vacuum reaction chamber and the discharge of residual precursors and/or by-products in the vacuum reaction chamber; and, in one implementation of the application, a dust filter is also provided between the vacuum pump 13 and the gas outlet 7 The device 12 is used to filter residual precursors and/or by-products and a small amount of dust brought by the carrier gas from the reaction chamber. The lower chamber hot oil inlet 8 and the lower chamber hot oil outlet 9 are opened on the lower chamber 1, the lower chamber hot oil inlet 8 is opened on the lower side of the lower chamber 1, and the lower chamber hot oil outlet 9 is opened on the lower side of the lower chamber. The upper side of the cavity 1 is used to connect the heating system. The heated hot oil enters through the hot oil inlet 8 of the lower cavity, and then is discharged from the hot oil outlet 9 of the lower cavity. During this process, the heat is transferred to the lower cavity 1, in order to realize the heating of the lower chamber 1. Similarly, the upper chamber hot oil inlet 10 and the upper chamber hot oil outlet 11 opened in the upper chamber 2 are also used to connect the heating system, and the upper chamber 2 is heated by the hot oil.
采用本例的气相原子层沉积装置对电极粉体材料进行包覆的方法,如图2所示,包括以下步骤:The method for coating the electrode powder material by using the vapor phase atomic layer deposition device of this example, as shown in Figure 2, includes the following steps:
(a)将待处理的电极粉体材料装入气相原子层沉积装置的真空反应腔体;(a) loading the electrode powder material to be processed into the vacuum reaction chamber of the vapor phase atomic layer deposition device;
(b)开启真空系统对真空反应腔体进行抽真空,维持真空反应腔体跟外部空气环境的有效隔离;(b) Turn on the vacuum system to evacuate the vacuum reaction chamber to maintain effective isolation between the vacuum reaction chamber and the external air environment;
(c)开启搅拌装置,利用搅拌装置将电极粉体材料扬起,使电极粉体材料充分分散;(c) Turn on the stirring device, and use the stirring device to raise the electrode powder material to fully disperse the electrode powder material;
(d)向真空反应腔体中通入第一种气相前驱体,使第一种气相前驱体吸附在电极粉体材料表面;脉冲时间为1-10秒,优选为1-5秒;(d) introducing the first gas phase precursor into the vacuum reaction chamber, so that the first gas phase precursor is adsorbed on the surface of the electrode powder material; the pulse time is 1-10 seconds, preferably 1-5 seconds;
(e)通入载气清洗反应腔体中过量的第一种气相前驱体,即清除没有吸附在电极粉体材料颗粒表面的第一种气相前驱体;在清洗的过程中,通常不需要停止搅拌,抽气口上装有孔径很小的过滤网,因此,电极粉体不会被抽走;(e) Pass the carrier gas to clean the excess first gas phase precursor in the reaction chamber, that is, remove the first gas phase precursor that is not adsorbed on the surface of the electrode powder material particles; during the cleaning process, it is usually not necessary to stop Stirring, the air suction port is equipped with a filter with a small pore size, so the electrode powder will not be sucked away;
(f)向真空反应腔体中通入第二种气相前驱体,脉冲时间为1-10秒,优选为1-5秒,使第二种气相前驱体与吸附在电极粉体材料表面的第一种气相前驱体反应,形成单原子层膜层;(f) feed the second gas phase precursor into the vacuum reaction chamber, the pulse time is 1-10 seconds, preferably 1-5 seconds, so that the second gas phase precursor and the first gas phase precursor adsorbed on the surface of the electrode powder material A gas-phase precursor reacts to form a monoatomic layer film;
(g)通入载气清洗反应腔体中过量的第二种气相前驱体,即清除没有参与反应的第二种气相前驱体以及第一种气相前驱体与第二种气相前驱体反应的副产物;(g) Passing the carrier gas to clean the excess second gas-phase precursor in the reaction chamber, that is, to remove the second gas-phase precursor that did not participate in the reaction and the side effects of the reaction between the first gas-phase precursor and the second gas-phase precursor product;
重复步骤(d)至(g)直到获得设定厚度的包覆层。Steps (d) to (g) are repeated until a cladding layer of a set thickness is obtained.
其中,步骤(d)或(f)中,根据待处理的电极粉体材料的颗粒大小和质量不同,调节搅拌装置的转速。具体的,对于原始粒径和质量大的微米级颗粒,调节搅拌装置转速为500-1000转每分钟,能够将电极粉体材料有效分散;对原始粒径和质量小的纳米级颗粒,调节搅拌装置转速为100-500转每分钟,能够将电极粉体材料有效分散。Wherein, in step (d) or (f), the rotational speed of the stirring device is adjusted according to the particle size and mass of the electrode powder material to be processed. Specifically, for micron-sized particles with a large original particle size and mass, adjust the rotation speed of the stirring device to 500-1000 revolutions per minute, which can effectively disperse the electrode powder material; for nano-sized particles with a small original particle size and mass, adjust the stirring The rotation speed of the device is 100-500 revolutions per minute, which can effectively disperse the electrode powder material.
对于第一种气相前驱体和第二种气相前驱体的脉冲时间,由于沉积过程需要一定时间使前驱体完全吸附在颗粒表面,如果脉冲时间小于1秒,则单次通入提供的前驱体量过少,不能有效包覆已经充分分散的电极粉体材料颗粒;而前驱体脉冲时间大于5秒,通入的前驱体被真空泵抽走,造成前驱体的浪费;因此,前驱体脉冲时间为1-10秒,优选为1-5秒。For the pulse time of the first gas-phase precursor and the second gas-phase precursor, since the deposition process requires a certain amount of time for the precursor to be completely adsorbed on the particle surface, if the pulse time is less than 1 second, the amount of precursor provided by a single injection If it is too small, the electrode powder material particles that have been fully dispersed cannot be effectively coated; if the pulse time of the precursor is greater than 5 seconds, the incoming precursor will be sucked away by the vacuum pump, resulting in waste of the precursor; therefore, the pulse time of the precursor is 1 - 10 seconds, preferably 1-5 seconds.
步骤(d)或(f)中,具体的,根据不同的前驱体对不同锂离子电池粉末颗粒表面吸附的难易程度,调节前驱体脉冲的通入次数,以10-20次为宜,通入次数太少,吸附的比例不高;通入次数太多,通入次数的增加对于前驱体吸附的贡献不大,且前驱体被真空泵抽走,造成前驱体的浪费。本例中前驱体脉冲是指,例如通入第一前驱体5秒,然后停止通入,再通入5秒,停止、通入5s,这样反复10次。需要说明的是,由于前驱体装在前驱体容器中,且具有一定的饱和蒸汽压;通入5秒,停止;待前驱体容器中压力恢复到饱和蒸汽压,再通入5秒;这样能够增加前驱体的载入量;每次5秒,10次脉冲,比单次通入50秒载入量要大很多。另外,暂停的时间通常在2秒左右即可。在通入前驱体的过程中,如果保压,则关闭真空泵,不保压则开启真空泵;具体采用保压吸附还是不保压吸附,可以根据各个前驱体的吸附难易程度而定。In step (d) or (f), specifically, according to the degree of difficulty of different precursors on the surface of different lithium-ion battery powder particles, adjust the number of precursor pulses, preferably 10-20 times, usually If the number of injections is too small, the ratio of adsorption is not high; if the number of injections is too large, the increase in the number of injections will not contribute much to the adsorption of the precursor, and the precursor is sucked away by the vacuum pump, resulting in waste of the precursor. In this example, the precursor pulse refers to, for example, feeding the first precursor for 5 seconds, then stopping the feeding, and then feeding it for 5 seconds, stopping and feeding it for 5 seconds, and repeating this 10 times. It should be noted that, since the precursor is contained in the precursor container, and has a certain saturated vapor pressure; pass through for 5 seconds, stop; wait for the pressure in the precursor container to return to the saturated vapor pressure, and then pass through for 5 seconds; this can Increase the loading amount of the precursor; 5 seconds each time, 10 pulses, which is much larger than the loading amount of a single pass of 50 seconds. In addition, the pause time is usually about 2 seconds. In the process of introducing the precursor, if the pressure is maintained, the vacuum pump is turned off, and if the pressure is not maintained, the vacuum pump is turned on; whether to use pressure-maintaining adsorption or not to maintain pressure adsorption can be determined according to the difficulty of adsorption of each precursor.
本例的加热系统对真空反应腔体的壁体进行加热,通过壁体的热量辐射加热真空反应腔体的内部,使其中的电极粉体材料颗粒达到反应条件所需的温度,该反应条件,即第一种气相前驱体和第二种气相前驱体的反应温度,通常该温度在50-300摄氏度之间,具体的反应温度根据具体的第一种气相前驱体和第二种气相前驱体而定。The heating system in this example heats the wall of the vacuum reaction chamber, and heats the interior of the vacuum reaction chamber through the heat radiation of the wall, so that the electrode powder material particles therein reach the temperature required by the reaction conditions. The reaction conditions, That is, the reaction temperature of the first gas-phase precursor and the second gas-phase precursor, usually the temperature is between 50-300 degrees Celsius, and the specific reaction temperature depends on the specific first gas-phase precursor and the second gas-phase precursor. Certainly.
另外,对于通入真空反应腔体的前驱体本身,其温度控制在25-200摄氏度。前驱体的熔点越高,其饱和蒸汽压越低,同等条件下获得的可以参与反应的前驱体量就越少。对于普通前驱体,温度控制在25-100摄氏度;对于熔点很高的固态前驱体,温度可以达到200摄氏度。前驱体管路的温度控制在25-200摄氏度,防止前驱体在输送管路中的冷凝。In addition, for the precursor itself that is passed into the vacuum reaction chamber, its temperature is controlled at 25-200 degrees Celsius. The higher the melting point of the precursor, the lower its saturated vapor pressure, and the less the amount of precursor that can participate in the reaction obtained under the same conditions. For ordinary precursors, the temperature is controlled at 25-100 degrees Celsius; for solid precursors with high melting points, the temperature can reach 200 degrees Celsius. The temperature of the precursor pipeline is controlled at 25-200 degrees Celsius to prevent condensation of the precursor in the delivery pipeline.
本申请中,前驱体可以是气态、液态、固态或等离子体态。液态或者固态前驱体可利用载气带入真空反应腔体,然后用纯的载气清洗;气态或等离子体态前驱体可以利用载气带入反应腔体,也可以直接通入真空反应腔体。In this application, the precursor may be in gaseous, liquid, solid or plasma state. Liquid or solid precursors can be brought into the vacuum reaction chamber with carrier gas, and then cleaned with pure carrier gas; gaseous or plasma state precursors can be brought into the reaction chamber with carrier gas, or directly into the vacuum reaction chamber.
本例的载气为惰性气体,优选为氮气。载气的温度为50-300摄氏度,一般来说,载气的温度与真空反应腔体内的反应温度相当,以减少对真空反应腔体内部反应区域温度均匀性的影响。The carrier gas in this example is an inert gas, preferably nitrogen. The temperature of the carrier gas is 50-300 degrees Celsius. Generally speaking, the temperature of the carrier gas is equivalent to the reaction temperature in the vacuum reaction chamber to reduce the influence on the temperature uniformity of the reaction area inside the vacuum reaction chamber.
试验1test 1
本试验以三甲基铝(缩写TMA)和水分别作为第一种前驱体和第二种前驱体,按照前面介绍的图2所示的步骤,对锂离子电池粉体材料进行包覆改性,具体的:In this experiment, trimethylaluminum (abbreviated as TMA) and water are used as the first precursor and the second precursor respectively, and the lithium-ion battery powder material is coated and modified according to the steps shown in Figure 2 introduced above. ,specific:
第一步:反应腔体装入的锂离子电池粉体材料为LiNiMnCoO2三元正极材料,正极材料的粒径约为10微米。Step 1: The lithium-ion battery powder material loaded into the reaction chamber is LiNiMnCoO 2 ternary cathode material, and the particle size of the cathode material is about 10 microns.
第二步:反应腔体抽真空,维持反应腔体对外部空气环境的有效隔离。其中,真空度达到100-300mTorr即可,本例具体的为200mTorr。The second step: the reaction chamber is vacuumed to maintain the effective isolation of the reaction chamber from the external air environment. Wherein, the degree of vacuum can reach 100-300mTorr, specifically 200mTorr in this example.
第三步:开启搅拌装置,搅拌装置的转速为500转每分钟,使不同质量和粒径的锂离子电池粉体材料得到充分分散。Step 3: Turn on the stirring device, and the rotating speed of the stirring device is 500 revolutions per minute, so that the lithium-ion battery powder materials of different masses and particle sizes are fully dispersed.
第四步:第一种气相前驱体三甲基铝TMA由载气N2辅助通入反应腔体,脉冲时间为1秒,TMA物理吸附在锂离子电池粉体颗粒的表面,通入TMA前驱体10次,该过程不对反应腔体抽气,提供100-300秒的较高压力的保压时间,本例具体的保压200秒,增加前驱体TMA与粉体颗粒表面的接触时间,以提高包覆均匀性以及包覆效率。Step 4: The first gas-phase precursor, trimethylaluminum TMA, is fed into the reaction chamber with the aid of carrier gas N2 , and the pulse time is 1 second. TMA is physically adsorbed on the surface of lithium-ion battery powder particles, and the TMA precursor is fed 10 times, the process does not pump the reaction chamber, and provides a higher pressure dwell time of 100-300 seconds. In this example, the specific dwell time is 200 seconds, increasing the contact time between the precursor TMA and the surface of the powder particles, so as to Improve coating uniformity and coating efficiency.
第五步:通入载气N2清洗反应腔体中过量的第一种气相前驱体,清除没有吸附在锂离子电池粉体颗粒表面的第一种气相前驱体,吹洗时间30秒。Step 5: Pass the carrier gas N2 to clean the excess first gas-phase precursor in the reaction chamber, and remove the first gas-phase precursor that is not adsorbed on the surface of the lithium-ion battery powder particles, and the purge time is 30 seconds.
第六步:第二种气相前驱体水,与第四步沉积TMA的方法相同,由载气氮气辅助将水蒸气通入反应腔体,同样保压200秒,水吸附在锂离子电池粉体颗粒表面并且与之前表面吸附的前驱体TMA发生化学反应,生成单原子层的膜层。Step 6: The second gas-phase precursor water is the same as the method for depositing TMA in the fourth step. The water vapor is assisted by the carrier gas nitrogen into the reaction chamber, and the pressure is also maintained for 200 seconds. The water is adsorbed on the lithium-ion battery powder The surface of the particle reacts chemically with the precursor TMA previously adsorbed on the surface to form a monoatomic layer film.
第七步:与第五步的清洗方法相同,除去未能与前驱体TMA反应的前驱体水以及前驱体TMA与前驱体水反应的副产物。因为水的粘滞性更强,可适当延长清洗时间,本例具体的延长清洗时间为2分钟。The seventh step: the same cleaning method as the fifth step, removing the precursor water that has not reacted with the precursor TMA and the by-products of the reaction between the precursor TMA and the precursor water. Because the viscosity of water is stronger, the cleaning time can be extended appropriately. In this example, the specific extended cleaning time is 2 minutes.
第八步:根据所需包覆改性层厚度,重复执行第四步至第七步,即可精确得到所需厚度的包覆改性层。本例具体重复了10次,最终制备出厚度约为3纳米的包覆改性层。Step 8: Repeat steps 4 to 7 according to the thickness of the coating modification layer required, and the coating modification layer of the desired thickness can be accurately obtained. This example was specifically repeated 10 times, and finally a coated modified layer with a thickness of about 3 nanometers was prepared.
利用透射电子显微镜TEM观察包覆前后颗粒的形貌,如图3所示。图3中(a)为包覆前的扫描结果,(b)为包覆后的扫描结果,可以看出包覆层清晰可见,厚度均匀,且具有高保型性。The morphology of the particles before and after coating was observed with a transmission electron microscope (TEM), as shown in Figure 3. In Figure 3, (a) is the scanning result before coating, and (b) is the scanning result after coating. It can be seen that the coating layer is clearly visible, uniform in thickness, and has high shape retention.
试验2test 2
本试验以二乙基锌(缩写DEZ)和水分别作为第一种前驱体和第二种前驱体,按照前面介绍的图2所示的步骤,对锂离子电池粉体材料进行包覆改性,具体的:In this experiment, diethyl zinc (abbreviated as DEZ) and water are used as the first precursor and the second precursor respectively, and the lithium-ion battery powder material is coated and modified according to the steps shown in Figure 2 introduced above. ,specific:
第一步:反应腔体装入的锂离子电池粉体材料为LiNiMnCoO2三元正极材料,正极材料的粒径约为10微米。Step 1: The lithium-ion battery powder material loaded into the reaction chamber is LiNiMnCoO 2 ternary cathode material, and the particle size of the cathode material is about 10 microns.
第二步:反应腔体抽真空,维持反应腔体对外部空气环境的有效隔离。其中,真空度达到100-300mTorr即可,本例具体的为200mTorr。The second step: the reaction chamber is vacuumed to maintain the effective isolation of the reaction chamber from the external air environment. Wherein, the degree of vacuum can reach 100-300mTorr, specifically 200mTorr in this example.
第三步:开启搅拌装置,搅拌装置的转速为500转每分钟,使不同质量和粒径的锂离子电池粉体材料得到充分分散。Step 3: Turn on the stirring device, and the rotating speed of the stirring device is 500 revolutions per minute, so that the lithium-ion battery powder materials of different masses and particle sizes are fully dispersed.
第四步:第一种气相前驱体二乙基锌DEZ由载气N2辅助通入反应腔体,脉冲时间为1秒,DEZ物理吸附在锂离子电池粉体颗粒的表面,通入DEZ前驱体10次,该过程不对反应腔体抽气,提供100-300秒的较高压力的保压时间,本例具体的保压200秒,增加前驱体DEZ与粉体颗粒表面的接触时间,以提高包覆均匀性以及包覆效率。Step 4: The first gas phase precursor, diethylzinc DEZ, is assisted by the carrier gas N 2 into the reaction chamber, and the pulse time is 1 second. DEZ is physically adsorbed on the surface of the lithium-ion battery powder particles, and the DEZ precursor is introduced In this process, the reaction chamber is not evacuated, and a higher pressure holding time of 100-300 seconds is provided. In this example, the specific holding pressure is 200 seconds, and the contact time between the precursor DEZ and the surface of the powder particle is increased to increase the contact time between the precursor DEZ and the powder particle surface. Improve coating uniformity and coating efficiency.
第五步:通入载气N2清洗反应腔体中过量的第一种气相前驱体,清除没有吸附在锂离子电池粉体颗粒表面的第一种气相前驱体,吹洗时间30秒。Step 5: Pass the carrier gas N2 to clean the excess first gas-phase precursor in the reaction chamber, and remove the first gas-phase precursor that is not adsorbed on the surface of the lithium-ion battery powder particles, and the purge time is 30 seconds.
第六步:第二种气相前驱体水H2O,与第四步沉积DEZ的方法相同,同样保压200秒,水吸附在锂离子电池粉体颗粒表面并且与之前表面吸附的前驱体DEZ发生化学反应,生成单原子层的膜层。Step 6: The second gas phase precursor, water H 2 O, is the same as the method for depositing DEZ in the fourth step. The pressure is also kept for 200 seconds. A chemical reaction occurs to form a monoatomic layer of film.
第七步:与第五步的清洗方法相同,除去未能与前驱体DEZ反应的前驱体水以及前驱体DEZ与前驱体水反应的副产物。因为水的粘滞性更强,可适当延长清洗时间,本例具体的延长清洗时间为2分钟。The seventh step: the same cleaning method as the fifth step, removing the precursor water that failed to react with the precursor DEZ and the by-products of the reaction between the precursor DEZ and the precursor water. Because the viscosity of water is stronger, the cleaning time can be extended appropriately. In this example, the specific extended cleaning time is 2 minutes.
第八步:根据所需包覆改性层厚度,重复执行第四步至第七步,即可精确得到所需厚度的包覆改性层。本例具体重复了10次,最终制备出厚度约为3纳米的包覆改性层。Step 8: Repeat steps 4 to 7 according to the thickness of the coating modification layer required, and the coating modification layer of the desired thickness can be accurately obtained. This example was specifically repeated 10 times, and finally a coated modified layer with a thickness of about 3 nanometers was prepared.
利用透射电子显微镜TEM观察包覆前后颗粒的形貌,可以看出包覆层清晰可见,厚度均匀,包覆均匀性好,具有高保型性;并且,包覆前后颗粒大小均匀,几乎没有团聚现象。Using a transmission electron microscope (TEM) to observe the morphology of the particles before and after coating, it can be seen that the coating layer is clearly visible, the thickness is uniform, the coating uniformity is good, and it has high shape retention; moreover, the particle size before and after coating is uniform, and there is almost no agglomeration phenomenon .
试验3Test 3
本试验以四(二甲氨基)钛(缩写TDMAT)和水分别作为第一种前驱体和第二种前驱体,按照前面介绍的图2所示的步骤,对锂离子电池粉体材料进行包覆改性,具体的:In this experiment, tetrakis(dimethylamino)titanium (abbreviated TDMAT) and water were used as the first precursor and the second precursor respectively, and the lithium-ion battery powder material was packaged according to the steps shown in Figure 2 introduced above. Modified, specifically:
第一步:反应腔体装入的锂离子电池粉体材料为LiNiMnCoO2三元正极材料,正极材料的粒径约为10微米。Step 1: The lithium-ion battery powder material loaded into the reaction chamber is LiNiMnCoO 2 ternary cathode material, and the particle size of the cathode material is about 10 microns.
第二步:反应腔体抽真空,维持反应腔体对外部空气环境的有效隔离。其中,真空度达到100-300mTorr即可,本例具体的为200mTorr。The second step: the reaction chamber is vacuumed to maintain the effective isolation of the reaction chamber from the external air environment. Wherein, the degree of vacuum can reach 100-300mTorr, specifically 200mTorr in this example.
第三步:开启搅拌装置,搅拌装置的转速为500转每分钟,使不同质量和粒径的锂离子电池粉体材料得到充分分散。Step 3: Turn on the stirring device, and the rotating speed of the stirring device is 500 revolutions per minute, so that the lithium-ion battery powder materials of different masses and particle sizes are fully dispersed.
第四步:第一种气相前驱体四(二甲氨基)钛TDMAT由载气N2辅助通入反应腔体,脉冲时间为1秒,TDMAT物理吸附在锂离子电池粉体颗粒的表面,通入TDMAT前驱体10次,该过程不对反应腔体抽气,提供100-300秒的较高压力的保压时间,本例具体的保压200秒,增加前驱体TDMAT与粉体颗粒表面的接触时间,以提高包覆均匀性以及包覆效率。The fourth step: the first gaseous phase precursor tetrakis(dimethylamino)titanium TDMAT is assisted by the carrier gas N 2 into the reaction chamber, the pulse time is 1 second, and TDMAT is physically adsorbed on the surface of the lithium-ion battery powder particles. Inject the TDMAT precursor 10 times. During this process, the reaction chamber is not pumped, and a higher pressure holding time of 100-300 seconds is provided. In this example, the specific holding pressure is 200 seconds to increase the contact between the precursor TDMAT and the surface of the powder particles. Time to improve coating uniformity and coating efficiency.
第五步:通入载气N2清洗反应腔体中过量的第一种气相前驱体,清除没有吸附在锂离子电池粉体颗粒表面的第一种气相前驱体,吹洗时间30秒。Step 5: Pass the carrier gas N2 to clean the excess first gas-phase precursor in the reaction chamber, and remove the first gas-phase precursor that is not adsorbed on the surface of the lithium-ion battery powder particles, and the purge time is 30 seconds.
第六步:第二种气相前驱体水H2O,与第四步沉积TDMAT的方法相同,同样保压200秒,水吸附在锂离子电池粉体颗粒表面并且与之前表面吸附的前驱体TDMAT发生化学反应,生成单原子层的膜层。Step 6: The second gas phase precursor, water H 2 O, is the same as the method for depositing TDMAT in the fourth step, and the pressure is also maintained for 200 seconds. A chemical reaction occurs to form a monoatomic layer of film.
第七步:与第五步的清洗方法相同,除去未能与前驱体TDMAT反应的前驱体水以及前驱体TDMAT与前驱体水反应的副产物。因为水的粘滞性更强,可适当延长清洗时间,本例具体的延长清洗时间为2分钟。The seventh step: the same cleaning method as the fifth step, removing the precursor water that failed to react with the precursor TDMAT and the by-products of the reaction between the precursor TDMAT and the precursor water. Because the viscosity of water is stronger, the cleaning time can be extended appropriately. In this example, the specific extended cleaning time is 2 minutes.
第八步:根据所需包覆改性层厚度,重复执行第四步至第七步,即可精确得到所需厚度的包覆改性层。本例具体重复了60次,最终制备出厚度约为3纳米的包覆改性层。Step 8: Repeat steps 4 to 7 according to the thickness of the coating modification layer required, and the coating modification layer of the desired thickness can be accurately obtained. This example was repeated 60 times, and finally a coated modified layer with a thickness of about 3 nanometers was prepared.
利用透射电子显微镜TEM观察包覆前后颗粒的形貌,可以看出包覆层清晰可见,厚度均匀,包覆均匀性好,具有高保型性;并且,包覆前后颗粒大小均匀,几乎没有团聚现象。Using a transmission electron microscope (TEM) to observe the morphology of the particles before and after coating, it can be seen that the coating layer is clearly visible, the thickness is uniform, the coating uniformity is good, and it has high shape retention; moreover, the particle size before and after coating is uniform, and there is almost no agglomeration phenomenon .
试验4Test 4
本试验以三(二乙基氨基)叔丁酰胺钽(缩写TBTDET)和水分别作为第一种前驱体和第二种前驱体,按照前面介绍的图2所示的步骤,对锂离子电池粉体材料进行包覆改性,具体的:In this experiment, tantalum tris(diethylamino)tert-butyramide (abbreviated TBTDET) and water were used as the first precursor and the second precursor respectively. Coating modification of body materials, specifically:
第一步:反应腔体装入的锂离子电池粉体材料为LiNiMnCoO2三元正极材料,正极材料的粒径约为10微米。Step 1: The lithium-ion battery powder material loaded into the reaction chamber is LiNiMnCoO 2 ternary cathode material, and the particle size of the cathode material is about 10 microns.
第二步:反应腔体抽真空,维持反应腔体对外部空气环境的有效隔离。其中,真空度达到100-300mTorr即可,本例具体的为200mTorr。The second step: the reaction chamber is vacuumed to maintain the effective isolation of the reaction chamber from the external air environment. Wherein, the degree of vacuum can reach 100-300mTorr, specifically 200mTorr in this example.
第三步:开启搅拌装置,搅拌装置的转速为500转每分钟,使不同质量和粒径的锂离子电池粉体材料得到充分分散。Step 3: Turn on the stirring device, and the rotating speed of the stirring device is 500 revolutions per minute, so that the lithium-ion battery powder materials of different masses and particle sizes are fully dispersed.
第四步:第一种气相前驱体三(二乙基氨基)叔丁酰胺钽TBTDET由载气N2辅助通入反应腔体,脉冲时间为1秒,TBTDET物理吸附在锂离子电池粉体颗粒的表面,通入TBTDET前驱体10次,该过程不对反应腔体抽气,提供100-300秒的较高压力的保压时间,本例具体的保压200秒,增加前驱体TBTDET与粉体颗粒表面的接触时间,以提高包覆均匀性以及包覆效率。Step 4: The first gaseous precursor tris(diethylamino)tert-butyramide tantalum TBTDET is assisted by the carrier gas N 2 into the reaction chamber, the pulse time is 1 second, and TBTDET is physically adsorbed on the lithium-ion battery powder particles The surface of the TBTDET precursor is injected 10 times. In this process, the reaction chamber is not pumped, and a higher pressure holding time of 100-300 seconds is provided. In this example, the specific holding pressure is 200 seconds, and the precursor TBTDET and powder are added. The contact time of the particle surface to improve coating uniformity and coating efficiency.
第五步:通入载气N2清洗反应腔体中过量的第一种气相前驱体,清除没有吸附在锂离子电池粉体颗粒表面的第一种气相前驱体,吹洗时间30秒。Step 5: Pass the carrier gas N2 to clean the excess first gas-phase precursor in the reaction chamber, and remove the first gas-phase precursor that is not adsorbed on the surface of the lithium-ion battery powder particles, and the purge time is 30 seconds.
第六步:第二种气相前驱体水H2O,与第四步沉积TBTDET的方法相同,同样保压200秒,水吸附在锂离子电池粉体颗粒表面并且与之前表面吸附的前驱体TBTDET发生化学反应,生成单原子层的膜层。Step 6: The second gas phase precursor, water H 2 O, is the same as the method for depositing TBTDET in the fourth step, and the pressure is also maintained for 200 seconds. A chemical reaction occurs to form a monoatomic layer of film.
第七步:与第五步的清洗方法相同,除去未能与前驱体TBTDET反应的前驱体水以及前驱体TBTDET与前驱体水反应的副产物。因为水的粘滞性更强,可适当延长清洗时间,本例具体的延长清洗时间为2分钟。The seventh step: the same cleaning method as the fifth step, removing the precursor water that failed to react with the precursor TBTDET and the by-products of the reaction between the precursor TBTDET and the precursor water. Because the viscosity of water is stronger, the cleaning time can be extended appropriately. In this example, the specific extended cleaning time is 2 minutes.
第八步:根据所需包覆改性层厚度,重复执行第四步至第七步,即可精确得到所需厚度的包覆改性层。本例具体重复了10次,最终制备出厚度约为1纳米的包覆改性层。Step 8: Repeat steps 4 to 7 according to the thickness of the coating modification layer required, and the coating modification layer of the desired thickness can be accurately obtained. This example was specifically repeated 10 times, and finally a coated modified layer with a thickness of about 1 nanometer was prepared.
利用透射电子显微镜TEM观察包覆前后颗粒的形貌,可以看出包覆层清晰可见,厚度均匀,包覆均匀性好,具有高保型性;并且,包覆前后颗粒大小均匀,几乎没有团聚现象。Using a transmission electron microscope (TEM) to observe the morphology of the particles before and after coating, it can be seen that the coating layer is clearly visible, the thickness is uniform, the coating uniformity is good, and it has high shape retention; moreover, the particle size before and after coating is uniform, and there is almost no agglomeration phenomenon .
试验5Test 5
本试验以四(乙基甲基胺基)铪(缩写TEMAH)和水分别作为第一种前驱体和第二种前驱体,按照前面介绍的图2所示的步骤,对锂离子电池粉体材料进行包覆改性,具体的:In this experiment, four (ethylmethylamino) hafnium (abbreviated as TEMAH) and water were used as the first precursor and the second precursor respectively. The material is coated and modified, specifically:
第一步:反应腔体装入的锂离子电池粉体材料为LiNiMnCoO2三元正极材料,正极材料的粒径约为10微米。Step 1: The lithium-ion battery powder material loaded into the reaction chamber is LiNiMnCoO 2 ternary cathode material, and the particle size of the cathode material is about 10 microns.
第二步:反应腔体抽真空,维持反应腔体对外部空气环境的有效隔离。其中,真空度达到100-300mTorr即可,本例具体的为200mTorr。The second step: the reaction chamber is vacuumed to maintain the effective isolation of the reaction chamber from the external air environment. Wherein, the degree of vacuum can reach 100-300mTorr, specifically 200mTorr in this example.
第三步:开启搅拌装置,搅拌装置的转速为500转每分钟,使不同质量和粒径的锂离子电池粉体材料得到充分分散。Step 3: Turn on the stirring device, and the rotating speed of the stirring device is 500 revolutions per minute, so that the lithium-ion battery powder materials of different masses and particle sizes are fully dispersed.
第四步:第一种气相前驱体四(乙基甲基胺基)铪TEMAH由载气N2辅助通入反应腔体,脉冲时间为1秒,TEMAH物理吸附在锂离子电池粉体颗粒的表面,通入TEMAH前驱体10次,该过程不对反应腔体抽气,提供100-300秒的较高压力的保压时间,本例具体的保压200秒,增加前驱体TEMAH与粉体颗粒表面的接触时间,以提高包覆均匀性以及包覆效率。Step 4: The first gas phase precursor tetrakis (ethylmethylamino) hafnium TEMAH is assisted by the carrier gas N 2 into the reaction chamber, the pulse time is 1 second, and TEMAH is physically adsorbed on the lithium-ion battery powder particles On the surface, the TEMAH precursor is injected 10 times. During this process, the reaction chamber is not pumped, and a relatively high pressure holding time of 100-300 seconds is provided. In this example, the specific holding pressure is 200 seconds, and the precursor TEMAH and powder particles are added. Surface contact time to improve coating uniformity and coating efficiency.
第五步:通入载气N2清洗反应腔体中过量的第一种气相前驱体,清除没有吸附在锂离子电池粉体颗粒表面的第一种气相前驱体,吹洗时间30秒。Step 5: Pass the carrier gas N2 to clean the excess first gas-phase precursor in the reaction chamber, and remove the first gas-phase precursor that is not adsorbed on the surface of the lithium-ion battery powder particles, and the purge time is 30 seconds.
第六步:第二种气相前驱体水H2O,与第四步沉积TEMAH的方法相同,同样保压200秒,水吸附在锂离子电池粉体颗粒表面并且与之前表面吸附的前驱体TEMAH发生化学反应,生成单原子层的膜层。Step 6: The second gas phase precursor, water H 2 O, is the same as the method for depositing TEMAH in the fourth step, and the pressure is also maintained for 200 seconds. A chemical reaction occurs to form a monoatomic layer of film.
第七步:与第五步的清洗方法相同,除去未能与前驱体TEMAH反应的前驱体水以及前驱体TEMAH与前驱体水反应的副产物。因为水的粘滞性更强,可适当延长清洗时间,本例具体的延长清洗时间为2分钟。The seventh step: the same cleaning method as the fifth step, remove the precursor water that has not reacted with the precursor TEMAH and the by-products of the reaction between the precursor TEMAH and the precursor water. Because the viscosity of water is stronger, the cleaning time can be extended appropriately. In this example, the specific extended cleaning time is 2 minutes.
第八步:根据所需包覆改性层厚度,重复执行第四步至第七步,即可精确得到所需厚度的包覆改性层。本例具体重复了50次,最终制备出厚度约为3纳米的包覆改性层。Step 8: Repeat steps 4 to 7 according to the thickness of the coating modification layer required, and the coating modification layer of the desired thickness can be accurately obtained. This example was repeated 50 times, and finally a coating modification layer with a thickness of about 3 nanometers was prepared.
利用透射电子显微镜TEM观察包覆前后颗粒的形貌,可以看出包覆层清晰可见,厚度均匀,包覆均匀性好,具有高保型性;并且,包覆前后颗粒大小均匀,几乎没有团聚现象。Using a transmission electron microscope (TEM) to observe the morphology of the particles before and after coating, it can be seen that the coating layer is clearly visible, the thickness is uniform, the coating uniformity is good, and it has high shape retention; moreover, the particle size before and after coating is uniform, and there is almost no agglomeration phenomenon .
本例的用于锂离子电池电极粉体材料包覆改性的气相原子层沉积装置通过引入搅拌装置,独立的调节搅拌装置的转速实现不同粒径和质量的锂离子电池电极粉体材料的充分分散,有效减轻粉体的团聚程度,利于前驱体的吸附和反应,提高了包覆均匀性以及包覆效率,适用于大规模高质量沉积。The vapor phase atomic layer deposition device used for the coating and modification of lithium-ion battery electrode powder materials in this example introduces a stirring device and independently adjusts the rotation speed of the stirring device to achieve sufficient particle size and quality of lithium-ion battery electrode powder materials. Dispersion can effectively reduce the degree of powder agglomeration, facilitate the adsorption and reaction of precursors, improve the coating uniformity and coating efficiency, and is suitable for large-scale high-quality deposition.
以上内容是结合具体的实施方式对本申请所作的进一步详细说明,不能认定本申请的具体实施只局限于这些说明。对于本申请所属技术领域的普通技术人员来说,在不脱离本申请构思的前提下,还可以做出若干简单推演或替换,都应当视为属于本申请的保护范围。The above content is a further detailed description of the present application in conjunction with specific implementation modes, and it cannot be considered that the specific implementation of the present application is limited to these descriptions. For those of ordinary skill in the technical field to which this application belongs, some simple deduction or substitutions can be made without departing from the concept of this application, which should be deemed to belong to the protection scope of this application.
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