CN116018698A - A kind of electrode structure and the method for manufacturing this electrode structure - Google Patents
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Abstract
描述了一种用于碱金属离子电池的电极结构。该电极结构包括能够承载碱金属离子的固体电解质;与固体电解质相邻的电极以及与电极相邻的电极集流体,所述电极能够在其中电极具有第一碱金属离子含量的第一状态和其中电极具有高于第一碱金属含量的第二碱金属离子含量的第二状态之间转换。在第一状态下,该电极包括:第一电极层,该第一电极层包括与电解质相邻的能够与碱金属合金化的第一材料,该第一材料具有第一碱金属离子含量A1。在第二状态下,该电极包括:第一电极层,包括第一材料和碱金属的合金,该合金具有高于第一碱金属离子含量A1的第二碱金属离子含量A2,以及在第一电极层和电极集流体之间的第二电极层,第二电极层包括碱金属。
An electrode structure for an alkali metal ion battery is described. The electrode structure includes a solid electrolyte capable of supporting alkali metal ions; an electrode adjacent to the solid electrolyte and an electrode current collector adjacent to the electrode capable of being in a first state wherein the electrode has a first alkali metal ion content and wherein The electrode transitions between a second state having a second alkali metal ion content higher than the first alkali metal content. In the first state, the electrode comprises: a first electrode layer comprising a first material capable of alloying with an alkali metal adjacent to the electrolyte, the first material having a first alkali metal ion content A . In the second state, the electrode comprises: a first electrode layer comprising an alloy of a first material and an alkali metal having a second alkali metal ion content A2 higher than the first alkali metal ion content A1 , and at The second electrode layer between the first electrode layer and the electrode collector, the second electrode layer includes an alkali metal.
Description
技术领域technical field
本发明涉及碱金属离子电池的电极结构、包含该电极结构的电池以及制造这种电极结构的方法。The present invention relates to electrode structures for alkali metal ion batteries, batteries comprising such electrode structures and methods of making such electrode structures.
背景技术Background technique
固体电池结构通常包括由固体电解质隔开的阳极层和阴极层。固体电解质包含碱金属离子,例如锂离子,并且在电池充电和放电时,碱金属离子经由固体电解质在阳极和阴极之间迁移。集流体可以用于阳极和阴极中的每一个,以收集电流并将其传导到电池内的适当点。集流体通常由诸如过渡金属的导电材料制成,并且通常以箔的形式提供,该箔放置在电极上并与电极电接触。A solid battery structure typically includes an anode layer and a cathode layer separated by a solid electrolyte. The solid electrolyte contains alkali metal ions, such as lithium ions, and the alkali metal ions migrate between the anode and the cathode through the solid electrolyte when the battery is charged and discharged. Current collectors can be used for each of the anode and cathode to collect and conduct electrical current to appropriate points within the battery. The current collector is usually made of a conductive material such as a transition metal, and is usually provided in the form of a foil that is placed over and in electrical contact with the electrodes.
阳极可以由例如碱金属层组成。在这种情况下,在电池充电期间,来自电解质的碱金属离子增加碱金属阳极的体积。The anode may consist, for example, of an alkali metal layer. In this case, during charging of the battery, alkali metal ions from the electrolyte increase the volume of the alkali metal anode.
然而,碱金属是难以处理的高活性材料。因此,制造含有碱金属的电极是困难的,并且既危险又昂贵。However, alkali metals are highly active materials that are difficult to handle. Therefore, making electrodes containing alkali metals is difficult, dangerous and expensive.
希望生产一种避免与已知电池结构相关的一个或多个问题的电池。It would be desirable to produce a battery that avoids one or more of the problems associated with known battery structures.
发明内容Contents of the invention
在此背景下,本发明涉及一种用于碱金属离子电池的电极结构,该电极结构包括:能够承载碱金属离子的固体电解质;与固体电解质相邻的电极以及与电极相邻的电极集流体,所述电极能够在其中电极具有第一碱金属离子含量的第一状态和其中电极具有高于第一碱金属含量的第二碱金属离子含量的第二状态之间转换。在第一状态下,电极包括第一电极层,第一电极层包括与电解质相邻的能够与碱金属合金化的第一材料,第一材料具有第一碱金属离子含量A1;并且在第二状态下,电极包括第一电极层和第二电极层,第一电极层包括第一材料和碱金属的合金,该合金具有高于第一碱金属离子含量A1的第二碱金属离子含量A2,第二电极层位于第一电极层和电极集流体之间,第二电极层包括碱金属。Against this background, the present invention relates to an electrode structure for an alkali metal ion battery comprising: a solid electrolyte capable of carrying alkali metal ions; an electrode adjacent to the solid electrolyte and an electrode current collector adjacent to the electrode , the electrode is switchable between a first state in which the electrode has a first alkali metal ion content and a second state in which the electrode has a second alkali metal ion content higher than the first alkali metal content. In the first state, the electrode comprises a first electrode layer comprising a first material capable of alloying with an alkali metal adjacent to the electrolyte, the first material having a first alkali metal ion content A 1 ; and in the In the second state, the electrode includes a first electrode layer and a second electrode layer, the first electrode layer includes an alloy of a first material and an alkali metal, the alloy has a second alkali metal ion content higher than the first alkali metal ion content A 1 A 2 , the second electrode layer is located between the first electrode layer and the electrode collector, and the second electrode layer includes alkali metal.
在第一电极层和电极集流体层之间的边界处形成碱金属的电镀层是形成碱金属层的特别有利的方式。第一电极层充当控制碱金属层的形成速率的“缓冲器”。因为第一电极材料与碱金属合金化,为了到达边界,碱金属离子不仅需要扩散通过第一阳极层,而且需要与层中的材料合金化,这显著减慢了电镀过程的动力学,同时热力学稳定。电镀层的较慢生长速率提供了均匀的碱金属层,避免了枝晶生长,这导致均匀的电镀,提高了电极的效率和性能。Forming a plating layer of alkali metal at the boundary between the first electrode layer and the electrode current collector layer is a particularly advantageous way of forming the alkali metal layer. The first electrode layer acts as a "buffer" controlling the rate of formation of the alkali metal layer. Because the first electrode material is alloyed with the alkali metal, in order to reach the boundary, the alkali metal ions not only need to diffuse through the first anodic layer, but also need to alloy with the material in the layer, which significantly slows down the kinetics of the plating process, while the thermodynamic Stablize. The slower growth rate of the plated layer provides a uniform alkali metal layer, avoiding dendrite growth, which results in uniform plating, improving the efficiency and performance of the electrode.
当形成第一电极材料的晶体结构,特别是晶系,可以认为由合金化机制导致的第一电极材料和第二电极材料之间的转换生效。这也可以表示为空间群或点群的变化。因此,第一电极材料和第二电极材料的区别在于它们具有不同的晶系、空间群或点群。When the crystal structure, especially the crystal system, of the first electrode material is formed, it can be considered that the transformation between the first electrode material and the second electrode material caused by the alloying mechanism takes effect. This can also be expressed as a change in the space group or point group. Therefore, the first electrode material and the second electrode material differ in that they have different crystal systems, space groups or point groups.
电极可以是阳极。所描述的电极结构特别适用于将被结合到电化学电池中的阳极结构。当电极是阳极时,第一状态可以对应于“放电”(或部分放电)状态,并且第二状态可以对应于“充电”(或部分充电)状态。The electrode can be an anode. The described electrode structures are particularly suitable for anode structures to be incorporated into electrochemical cells. When the electrode is an anode, the first state may correspond to a "discharged" (or partially discharged) state, and the second state may correspond to a "charged" (or partially charged) state.
第一电极材料优选选自:锡、锡锗、铋、银、铝、锌、锗或磷化锂。这种材料是安全、有效的,并且相对容易制造,例如使用物理气相沉积(PVD)技术。The first electrode material is preferably selected from: tin, tin germanium, bismuth, silver, aluminum, zinc, germanium or lithium phosphide. The material is safe, effective, and relatively easy to manufacture, for example using physical vapor deposition (PVD) techniques.
第一电极层可以是PVD沉积层。PVD是用于产生电池结构,特别是用于产生分层结构的特别方便的方法。The first electrode layer may be a PVD deposited layer. PVD is a particularly convenient method for producing battery structures, especially for producing layered structures.
电极集流体优选包括沉积在电极上的沉积层。这提供了电极集流体和电极之间的紧密接触,使得电极集流体层的效率和有效性最大化、损耗最小化,并且还允许电极集流体层提供特别有效的保护,防止碱金属通过电极表面的反应而损失。The electrode current collector preferably includes a deposition layer deposited on the electrode. This provides an intimate contact between the electrode collector and the electrode, maximizing the efficiency and effectiveness of the electrode collector layer, minimizing losses, and also allowing the electrode collector layer to provide particularly effective protection against the passage of alkali metals through the electrode surface loss in response.
电极集流体层可以抵抗与碱金属形成合金。以这种方式,碱金属将不会被带入集流体层,在那里它将不再有助于电池的容量,而是将保留在第一和第二阳极层中。这也防止碱金属通过电极集流体层损失。优选地,电极集流体层包括过渡金属,最优选地选自:铜、铂、镍、钼和钨。这些材料是易于生产的有效集流体层。The electrode current collector layer can resist alloying with alkali metals. In this way, the alkali metal will not be carried into the current collector layer, where it will no longer contribute to the capacity of the battery, but will remain in the first and second anode layers. This also prevents loss of alkali metal through the electrode current collector layer. Preferably, the electrode current collector layer comprises a transition metal, most preferably selected from: copper, platinum, nickel, molybdenum and tungsten. These materials are effective current collector layers that are easy to produce.
在第一状态下,电极可以包括位于第一电极层和电极集流体之间的第二电极层,第二电极层包括碱金属。第二层在第一状态下的厚度可以大于在第二状态下的厚度。在这种情况下,第二电极层(即碱金属层)的某些部分保持在第一状态。这可能是由于寄生损耗导致一定量的第二层始终剩余。替代地,这可能是因为第一状态是仅一部分碱金属含量已经从电极移除的状态(例如通过电极的充电或放电),使得一些碱金属层残留。在这种情况下,如果需要,碱金属离子的进一步移除可以在未来的点发生,在这种情况下,碱金属层可以被去除。In the first state, the electrode may include a second electrode layer between the first electrode layer and the electrode collector, the second electrode layer including an alkali metal. The thickness of the second layer in the first state may be greater than in the second state. In this case, some portion of the second electrode layer (ie, the alkali metal layer) remains in the first state. This may be due to parasitic losses where a certain amount of second layer is always left. Alternatively, this may be because the first state is a state in which only a portion of the alkali metal content has been removed from the electrode (eg by charging or discharging of the electrode), so that some alkali metal layer remains. In this case, further removal of alkali metal ions can take place at a future point, if desired, in which case the alkali metal layer can be removed.
在第一状态下,第一电极材料的碱金属含量A1可以小于1at%,优选为基本上0at%。换句话说,在第一状态下,第一电极层可以基本上不含处于第一状态的碱金属离子。这是有利的,因为它最大化了电极的容量,并因此最大化了电极结合到其中的电池的容量。In the first state, the alkali metal content A1 of the first electrode material may be less than 1 at%, preferably substantially 0 at%. In other words, in the first state, the first electrode layer may be substantially free of alkali metal ions in the first state. This is advantageous because it maximizes the capacity of the electrodes, and thus the capacity of the battery into which the electrodes are incorporated.
碱金属可以是例如锂和/或钠。锂和钠是特别优选的,因为它们很轻但反应性很高,因此提供了高能量密度电池。钠和锂也有利地嵌入。在一些情况下,锂可能是特别优选的,因为它具有特别高的能量密度。在其他情况下,钠可能是特别优选的,因为它是一种反应性较低,因此有害性较低的材料,更容易处理。Alkali metals may be, for example, lithium and/or sodium. Lithium and sodium are particularly preferred because they are light but highly reactive, thus providing high energy density batteries. Sodium and lithium also intercalate favorably. Lithium may be particularly preferred in some cases because of its particularly high energy density. In other cases sodium may be particularly preferred as it is a less reactive and therefore less hazardous material that is easier to handle.
本发明还延伸到碱金属离子电池,其包括上述电极结构和邻近固体电解质的另一电极。在所述电极是阳极的情况下,所述另一电极可以是阴极。以这种方式,电极可以结合到可以用于为设备供电的电池中。The invention also extends to an alkali metal ion battery comprising the electrode structure described above and a further electrode adjacent to a solid electrolyte. In case the electrode is an anode, the other electrode may be a cathode. In this way, the electrodes can be incorporated into batteries that can be used to power devices.
第一电极层可以具有由第一电极材料和/或第一电极层的厚度确定的第一碱金属离子存量I1。另一电极可以具有由另一电极材料和/或另一电极层的厚度确定的第二碱金属离子存量I2。可以选择I1和I2,使得I1≤0.5I2。这样,第一电极层的碱金属离子存量小于或等于另一电极的碱金属离子存量的一半。这意味着,当所有碱金属离子已经从所述另一电极转移到所述电极时,最多一半的碱金属离子存量被第一电极层占据,因此被合金化机制占据,并且最小一半的碱金属离子存量可以用于形成第二电极层,即碱金属层。确保至少一半的碱金属存量可以用于碱金属层提供了高电池容量,因为通过电镀碱金属比通过合金化机制可以获得更大的容量。The first electrode layer may have a first alkali metal ion inventory I 1 determined by the first electrode material and/or the thickness of the first electrode layer. The further electrode may have a second alkali metal ion inventory I 2 determined by the further electrode material and/or the thickness of the further electrode layer. I 1 and I 2 can be chosen such that I 1 ≦0.5I 2 . In this way, the alkali metal ion inventory of the first electrode layer is less than or equal to half of the alkali metal ion inventory of the other electrode. This means that when all alkali metal ions have been transferred from said other electrode to said electrode, at most half of the stock of alkali metal ions is occupied by the first electrode layer and thus by the alloying mechanism, and at least half of the alkali metal The ion inventory can be used to form the second electrode layer, the alkali metal layer. Ensuring that at least half of the alkali metal inventory is available for the alkali metal layer provides high battery capacity since greater capacity can be achieved by electroplating alkali metal than by alloying mechanisms.
本发明进一步延伸到制造用于碱金属离子电池的电极结构的方法,该方法包括:提供包含碱金属离子的固体电解质层;在固体电解质层上沉积电极,该电极包括第一电极层,第一电极层包括能够与碱金属合金化的第一电极材料;以及在电极上沉积电极集流体层。这提供了制造上述电极结构的方便且有效的方法。The invention further extends to a method of making an electrode structure for an alkali metal ion battery, the method comprising: providing a solid electrolyte layer comprising alkali metal ions; depositing an electrode on the solid electrolyte layer, the electrode comprising a first electrode layer, a first The electrode layer includes a first electrode material capable of alloying with an alkali metal; and an electrode current collector layer is deposited on the electrode. This provides a convenient and efficient method of fabricating the electrode structures described above.
该方法可以包括使用物理气相沉积方法沉积电极层和/或电极集流体层。PVD是用于产生电池结构,特别是用于产生分层结构的特别方便的方法。The method may include depositing an electrode layer and/or an electrode current collector layer using a physical vapor deposition method. PVD is a particularly convenient method for producing battery structures, especially for producing layered structures.
该方法可以包括使电极结构处于基本上不含碱金属的状态。这有利地允许在不需要形成任何碱金属层或部件的情况下制造电极,否则碱金属层或部件将相对昂贵和危险。基本上不含碱金属的这种状态可以对应于例如放电状态,放电状态对于电极的制造来说可以是危险性较小的状态,并且可以允许在不需要额外放电步骤的情况下处理和销售电极。The method can include rendering the electrode structure substantially free of alkali metals. This advantageously allows the fabrication of electrodes without the need to form any alkali metal layers or features, which would otherwise be relatively expensive and dangerous. Such a state substantially free of alkali metals may correspond to, for example, a discharged state, which may be a less hazardous state for the manufacture of the electrode and may allow the electrode to be handled and sold without the need for an additional discharge step .
本发明还包括一种用于碱金属离子电池的电极结构,该电极结构包括:能够承载碱金属离子的固体电解质;与固体电解质相邻的电极以及与电极相邻的电极集流体,所述电极能够在其中电极具有第一碱金属离子含量的第一状态和其中电极具有高于第一碱金属含量的第二碱金属离子含量的第二状态之间转换。该电极包括邻近固体电解质的第一电极层,第一电极层包括第一电极材料和碱金属的合金;以及位于第一电极层和电极集流体之间的第二电极层,第二电极层包括碱金属。在第一状态下,第二电极层具有厚度t1,并且在第二状态下,第二电极层具有大于t1的厚度t2。The present invention also includes an electrode structure for an alkali metal ion battery, the electrode structure comprising: a solid electrolyte capable of carrying alkali metal ions; an electrode adjacent to the solid electrolyte and an electrode collector adjacent to the electrode, the electrode Switchable between a first state in which the electrode has a first alkali metal ion content and a second state in which the electrode has a second alkali metal ion content higher than the first alkali metal content. The electrode comprises a first electrode layer adjacent to the solid electrolyte, the first electrode layer comprising an alloy of a first electrode material and an alkali metal; and a second electrode layer positioned between the first electrode layer and an electrode current collector, the second electrode layer comprising alkali metal. In the first state the second electrode layer has a thickness t 1 and in the second state the second electrode layer has a thickness t 2 which is greater than t 1 .
在第一电极层和电极集流体层之间的边界处形成碱金属的电镀层是形成碱金属层的特别有利的方式。第一电极层充当控制碱金属层的形成速率的“缓冲器”。因为第一电极材料与碱金属合金化,为了到达边界,碱金属离子不仅需要扩散通过第一阳极层,而且需要与层中的材料合金化,这显著减慢了电镀过程的动力学,同时热力学稳定。电镀层的较慢生长速率提供了均匀的碱金属层,避免了枝晶生长,这导致均匀的电镀,提高了电极的效率和性能。Forming a plating layer of alkali metal at the boundary between the first electrode layer and the electrode current collector layer is a particularly advantageous way of forming the alkali metal layer. The first electrode layer acts as a "buffer" controlling the rate of formation of the alkali metal layer. Because the first electrode material is alloyed with the alkali metal, in order to reach the boundary, the alkali metal ions not only need to diffuse through the first anodic layer, but also need to alloy with the material in the layer, which significantly slows down the kinetics of the plating process, while the thermodynamic Stablize. The slower growth rate of the plated layer provides a uniform alkali metal layer, avoiding dendrite growth, which results in uniform plating, improving the efficiency and performance of the electrode.
当形成第一电极材料的晶体结构,特别是晶系,可以认为由合金化机制导致的第一电极材料和第二电极材料之间的转变生效。这也可以表示为空间群或点群的变化。因此,第一电极材料和第二电极材料的区别在于它们具有不同的晶系、空间群或点群。When the crystal structure, in particular the crystal system, of the first electrode material is formed, it can be considered that the transformation between the first electrode material and the second electrode material caused by the alloying mechanism takes effect. This can also be expressed as a change in the space group or point group. Therefore, the first electrode material and the second electrode material differ in that they have different crystal systems, space groups or point groups.
电极可以是阳极。所描述的电极结构特别适用于将被结合到电化学电池中的阳极结构。当电极是阳极时,第一状态可以对应于“放电”(或部分放电)状态,并且第二状态可以对应于“充电”(或部分充电)状态。The electrode can be an anode. The described electrode structures are particularly suitable for anode structures to be incorporated into electrochemical cells. When the electrode is an anode, the first state may correspond to a "discharged" (or partially discharged) state, and the second state may correspond to a "charged" (or partially charged) state.
第一电极材料优选选自:锡、锡锗、铋、银、铝、锌、锗或磷化锂。这种材料是安全、有效的,并且相对容易制造,例如使用物理气相沉积(PVD)技术。The first electrode material is preferably selected from: tin, tin germanium, bismuth, silver, aluminum, zinc, germanium or lithium phosphide. The material is safe, effective, and relatively easy to manufacture, for example using physical vapor deposition (PVD) techniques.
第一电极层可以是PVD沉积层。PVD是用于产生电池结构,特别是用于产生分层结构的特别方便的方法。The first electrode layer may be a PVD deposited layer. PVD is a particularly convenient method for producing battery structures, especially for producing layered structures.
电极集流体优选包括沉积在电极上的沉积层。这提供了电极集流体和电极之间的紧密接触,使得电极集流体层的效率和有效性最大化、损耗最小化,并且还允许电极集流体层提供特别有效的保护,防止碱金属通过电极表面的反应而损失。The electrode current collector preferably includes a deposition layer deposited on the electrode. This provides an intimate contact between the electrode collector and the electrode, maximizing the efficiency and effectiveness of the electrode collector layer, minimizing losses, and also allowing the electrode collector layer to provide particularly effective protection against the passage of alkali metals through the electrode surface loss in response.
电极集流体层可以抵抗与碱金属形成合金。以这种方式,碱金属将不会被带入集流体层,在那里它将不再有助于电池的容量,而是将保留在第一和第二阳极层中。这也防止碱金属通过电极集流体层损失。优选地,电极集流体层包括过渡金属,最优选地选自:铜、铂、镍、钼和钨。这些材料是易于生产的有效集流体层。The electrode current collector layer can resist alloying with alkali metals. In this way, the alkali metal will not be carried into the current collector layer, where it will no longer contribute to the capacity of the battery, but will remain in the first and second anode layers. This also prevents loss of alkali metal through the electrode current collector layer. Preferably, the electrode current collector layer comprises a transition metal, most preferably selected from: copper, platinum, nickel, molybdenum and tungsten. These materials are effective current collector layers that are easy to produce.
固体电极可以含有碱金属离子。Solid electrodes may contain alkali metal ions.
碱金属可以是例如锂和/或钠。锂和钠是特别优选的,因为它们很轻但反应性很高,因此提供了高能量密度电池。钠和锂也有利地嵌入。在一些情况下,锂可能是特别优选的,因为它具有特别高的能量密度。在其他情况下,钠可能是特别优选的,因为它是一种反应性较低,因此有害性较低的材料,更容易处理。Alkali metals may be, for example, lithium and/or sodium. Lithium and sodium are particularly preferred because they are light but highly reactive, thus providing high energy density batteries. Sodium and lithium also intercalate favorably. Lithium may be particularly preferred in some cases because of its particularly high energy density. In other cases sodium may be particularly preferred as it is a less reactive and therefore less hazardous material that is easier to handle.
本发明还延伸到碱金属离子电池,其包括上述电极结构和邻近固体电解质的另一电极。在所述电极是阳极的情况下,所述另一电极可以是阴极。以这种方式,电极可以结合到可以用于为设备供电的电池中。The invention also extends to an alkali metal ion battery comprising the electrode structure described above and a further electrode adjacent to a solid electrolyte. In case the electrode is an anode, the other electrode may be a cathode. In this way, the electrodes can be incorporated into batteries that can be used to power devices.
本发明还延伸到制造用于碱金属离子电池的电极结构的方法,该方法包括:提供包含碱金属离子的固体电解质层;在固体电解质层上沉积第一电极层,第一电极层包括i)能够与碱金属合金化的第一电极材料或ii)碱金属和第一电极材料的合金;在第一电极层上沉积第二电极层,第二电极层包括碱金属层;以及在第二电极层上沉积电极集流体层,电极集流体层包括抵抗与碱金属合金化的材料。该方法提供了制造上述电极的简便方法。The invention also extends to a method of making an electrode structure for an alkali metal ion battery, the method comprising: providing a solid electrolyte layer comprising alkali metal ions; depositing a first electrode layer on the solid electrolyte layer, the first electrode layer comprising i) a first electrode material capable of alloying with an alkali metal or ii) an alloy of an alkali metal and the first electrode material; depositing a second electrode layer on the first electrode layer, the second electrode layer comprising an alkali metal layer; and depositing on the second electrode An electrode current collector layer comprising a material resistant to alloying with an alkali metal is deposited on the layer. This method provides a facile method for fabricating the electrodes described above.
该方法可以包括使用物理气相沉积方法沉积电极层和/或电极集流体层。PVD是用于产生电池结构,特别是用于产生分层结构的特别方便的方法。The method may include depositing an electrode layer and/or an electrode current collector layer using a physical vapor deposition method. PVD is a particularly convenient method for producing battery structures, especially for producing layered structures.
该方法可以包括使电极结构处于第一状态。这有利地允许用相对低的碱金属离子含量制造电极。这可以对应于例如放电状态,放电状态对于电极的制造来说可以是危险性较小的状态,并且可以允许在不需要额外放电步骤的情况下处理和销售电极。The method may include placing the electrode structure in a first state. This advantageously allows the fabrication of electrodes with a relatively low content of alkali metal ions. This may correspond to, for example, a discharge state, which may be a less hazardous state for the manufacture of the electrode and may allow handling and sale of the electrode without the need for an additional discharge step.
在第一电极层包括i)能够与碱金属合金化的第一电极材料的实施例中,该方法可以进一步包括增加电极的碱金属离子含量的步骤,从而使第一电极材料与碱金属合金化以形成第二电极材料。这有利地允许最初当第一电极层处于非合金化状态时制造电极,这可能比制造合金化状态的层更容易,并且允许第一电极层经历随后的合金化过程。增加电极的碱金属离子含量的步骤可以包括给电极充电。In embodiments where the first electrode layer comprises i) a first electrode material capable of alloying with an alkali metal, the method may further comprise the step of increasing the alkali metal ion content of the electrode, thereby alloying the first electrode material with an alkali metal to form the second electrode material. This advantageously allows the electrode to be fabricated initially when the first electrode layer is in an unalloyed state, which may be easier than fabricating the layer in an alloyed state, and allows the first electrode layer to undergo a subsequent alloying process. The step of increasing the alkali metal ion content of the electrode may include charging the electrode.
上述任何一个方面或实施例的特征也可以单独应用或适当组合应用于其他方面和实施例的特征。The features of any one aspect or embodiment above can also be applied independently or in proper combination to the features of other aspects and embodiments.
附图说明Description of drawings
为了更容易理解本发明,现在将参考附图以示例的方式描述本发明的实施例,其中:For easier understanding of the invention, embodiments of the invention will now be described by way of example with reference to the accompanying drawings, in which:
图1是处于放电状态的根据第一实施例的电池的示意图;1 is a schematic diagram of a battery according to a first embodiment in a discharged state;
图2是处于充电状态的图1的电池的示意图;Figure 2 is a schematic diagram of the battery of Figure 1 in a charged state;
图3a至3c是制造图1的电池的方法中的阶段的示意图;Figures 3a to 3c are schematic illustrations of stages in a method of manufacturing the battery of Figure 1;
图4是处于放电状态的根据第二实施例的电池的示意图;Figure 4 is a schematic diagram of a battery according to a second embodiment in a discharged state;
图5是处于带电状态的图4的电池的示意图;Figure 5 is a schematic diagram of the battery of Figure 4 in a charged state;
图6是图4和5的电池在其制造点处于替代的放电状态的示意图;以及Figure 6 is a schematic illustration of the battery of Figures 4 and 5 in an alternate state of discharge at its point of manufacture; and
图7a至7c是制造图6的电池的方法中的阶段的示意图。7a to 7c are schematic diagrams of stages in a method of manufacturing the battery of FIG. 6 .
具体实施方式Detailed ways
图1和图2示出了用于诸如锂离子电池组或钠离子电池组的碱金属离子电池的电池10。Figures 1 and 2 illustrate a
电池包括两个电极:第一电极,这里称为阳极14,和另一或第二电极,这里称为阴极12。电极12、14被固体电解质16隔开。固体电解质16由碱金属离子在其中可扩散的材料制成,使得碱金属离子可以在阳极14和阴极12之间来回移动,用于电池10的充电和放电。固体电解质可以是任何合适的固体或半固体材料,例如离子传导聚合物、陶瓷、凝胶或包括固体或半固体基质材料的材料。The battery includes two electrodes: a first electrode, referred to herein as the
阳极集流体层22在阳极14上。在该示例中,阳极集流体层22直接沉积在阳极14上,使得其与阳极14紧密接触。An anode
阳极14可以在第一状态和第二状态之间转换,在第一状态中,阳极14具有相对低的碱金属离子含量,在这里称为放电状态并如图1所示,在第二状态中,阳极14具有相对高的碱金属离子含量,在这里称为充电状态并如图2所示。在这种情况下,图1示出了完全放电状态,图2示出了完全充电状态,尽管应当理解,阳极也可以处于部分充电状态。在碱金属为锂的情况下,第一或放电状态也可以称为脱锂状态,第二或充电状态也可以称为锂化状态。
在放电状态下,阳极14包括与电解质16相邻的第一阳极层24。第一阳极层24包括能够与电池的碱金属形成合金的第一材料26。第一材料26具有第一碱金属离子含量A1。In a discharged state,
在充电状态下,阳极14包括与电解质16相邻的第一阳极层24及位于第一阳极层24和阳极集流体层22之间的第二阳极层28。在该充电状态下,第一阳极层24包括不同于第一材料26的第二材料29,特别是第一材料26和碱金属的合金。第二材料29具有比第一碱金属离子含量A1高的第二碱金属离子含量A2。In a charged state,
第二阳极层28包括碱金属。The
如下面将更详细地解释的,电池10可以有利地在图1的放电状态下制造,其中阳极14基本上不含碱金属。在该状态下,阳极14仅包括碱金属离子含量A1基本上为0的第一阳极层24。换句话说,第一阳极层24基本上不含碱金属,但是能够与碱金属形成合金。As will be explained in more detail below,
当电池充电时,阳极经历两种阳极充电机制。这里顺序地描述了这些机制,但是应当理解,这些机制可以在某种程度上并行出现。When the battery is charging, the anode undergoes two mechanisms of anode charging. These mechanisms are described here sequentially, but it should be understood that these mechanisms may occur in parallel to some extent.
第一阳极充电机制是合金化机制。通过该机制,碱金属离子从电解质16扩散到第一阳极层24中,并与第一材料26合金化。最终,当足够的碱金属离子已经扩散到第一阳极层24中时,第一阳极材料26将已经与碱金属离子充分地合金化,并且第一阳极层24将被碱金属离子饱和。在该状态下,第一阳极层24现在将包括第二阳极材料29,第二阳极材料29是第一阳极材料26和碱金属的合金。The first anodic charging mechanism is the alloying mechanism. Through this mechanism, alkali metal ions diffuse from the
第二阳极材料29与第一阳极材料的区别在于,第二阳极材料29的碱金属离子含量A2大于第一阳极材料的第一碱金属离子含量A1。第二阳极材料29的区别还在于,经过合金化处理的第二阳极材料具有不同的晶体结构,特别是不同的晶系。作为非限制性示例,第一阳极材料26的晶系可以是立方的,第二阳极材料29的晶系可以是三角的。换句话说,合金材料的空间群或点群在第一材料26和第二材料29之间变化。因此,当材料的晶系、空间群或点群改变时,可以说第一和第二阳极材料26、29之间的转换发生。这种合金化机制是特别有利的,因为它是热力学稳定的。The difference between the second anode material 29 and the first anode material is that the alkali metal ion content A 2 of the second anode material 29 is greater than the first alkali metal ion content A 1 of the first anode material. The difference of the second anode material 29 also lies in that the alloyed second anode material has different crystal structures, especially different crystal systems. As a non-limiting example, the crystal system of the first anode material 26 may be cubic and the crystal system of the second anode material 29 may be trigonal. In other words, the space group or point group of the alloy material varies between the first material 26 and the second material 29 . Thus, a transition between the first and second anode materials 26, 29 can be said to occur when the crystal system, space group or point group of the material is changed. This alloying mechanism is particularly advantageous because it is thermodynamically stable.
第二阳极充电机制是碱金属电镀机制。随着充电的继续,更多的碱金属离子扩散到第一阳极层24中。然而,一旦第一阳极层24被碱金属离子饱和,这些离子就不能再容纳在第一阳极层24中。相反,碱金属离子将扩散到第一阳极层24和集流体层22之间的边界30。选择集流体层22的材料,使得其能够抵抗与碱金属形成合金,并且能够抵抗碱金属离子的扩散。因此,碱金属将被“电镀”在第一阳极层24和集流体层22之间的边界30处。该电镀形成包括碱金属的第二阳极层28。The second anodic charging mechanism is the alkali metal plating mechanism. As charging continues, more alkali metal ions diffuse into the first anode layer 24 . However, once the first anode layer 24 is saturated with alkali metal ions, these ions can no longer be accommodated in the first anode layer 24 . Instead, the alkali metal ions will diffuse to the boundary 30 between the first anode layer 24 and the
当阴极的基本上全部碱金属离子存量已经转移到阳极时(或者作为第一阳极层24的合金的一部分,或者作为第二阳极层28的电镀碱金属的一部分),充电完成。在这种状态下,电池已经准备好用于放电。Charging is complete when substantially the entire inventory of alkali metal ions at the cathode has been transferred to the anode (either as part of the alloy of the first anode layer 24 or as part of the plated alkali metal of the second anode layer 28). In this state, the battery is ready for discharge.
在放电期间,将发生反向阳极机制:具体地,i)脱合金机制,通过该脱合金机制,碱金属离子将扩散出第一阳极层24到达固体电解质16,最终使第二材料29脱合金回到第一材料26,以及ii)脱镀机制,通过该脱镀机制,第二阳极层28的碱金属通过第一阳极层24扩散回到固体电解质16。这将第二阳极层28的厚度从充电状态下的厚度t2减小到放电状态下的厚度t1。在该示例中,厚度t1基本上为0。During discharge, reverse anode mechanisms will occur: specifically, i) a dealloying mechanism by which alkali metal ions will diffuse out of the first anode layer 24 to the
在第一阳极层24和阳极集流体层22之间的边界30处形成碱金属电镀层是形成碱金属层28的特别有利的方式。第一阳极层24充当控制碱金属层28的形成速率的“缓冲器”。特别地,为了到达边界30,碱金属离子不仅需要扩散通过第一阳极层,而且还需要与该层中的材料合金化,这显著减慢了电镀过程的动力学。电镀层的较慢生长速率提供了避免枝晶生长的均匀碱金属层。这是特别有利的,因为否则枝晶会“阻塞”电解质的表面积,防止扩散并降低电镀过程的效率,从而降低电极的效率。枝晶还具有比周围表面更高的表面能,使得当存在枝晶时,电镀优先发生在枝晶上,导致不均匀的层。因此,不存在枝晶提高了电池的效率和性能。Forming an alkali metal plating layer at the boundary 30 between the first anode layer 24 and the anode
更详细地考虑阳极层:Consider the anode layer in more detail:
第一阳极层24的第一材料26被选择为能够与碱金属合金化。因此,第一材料的性质取决于电池的碱金属。合适的材料包括例如:硅(Si)、锡(Sn)、锗(Ge)、铅(Pb)、砷(As)、铟(In)、金(Au)、银(Ag)、镉(Cd)、铝(Al)、锌(Zn)、铋(Bi)、含铋化合物、磷酸锂(LixP)、锡、锗或硅基合金(Sn-M、Ge-M、Si-M,其中M是G2-G7原子)、过渡金属基化合物(例如Tm-P、TmSby、Tm-Zn,其中Tm是过渡金属),以及导电过渡金属氧化物(例如FexOy、NiO、CoO、MnO2、Cr2O3、CuO)。The first material 26 of the first anode layer 24 is selected to be capable of alloying with an alkali metal. Therefore, the properties of the first material depend on the alkali metal of the cell. Suitable materials include, for example: silicon (Si), tin (Sn), germanium (Ge), lead (Pb), arsenic (As), indium (In), gold (Au), silver (Ag), cadmium (Cd) , aluminum (Al), zinc (Zn), bismuth (Bi), bismuth-containing compounds, lithium phosphate (Li x P), tin, germanium or silicon-based alloys (Sn-M, Ge-M, Si-M, where M are G2-G7 atoms), transition metal-based compounds (such as Tm-P, TmSby y , Tm-Zn, where Tm is a transition metal), and conductive transition metal oxides (such as F x O y , NiO, CoO, MnO 2 , Cr 2 O 3 , CuO).
可特别适用于锂离子电池的特别优选的材料包括例如:锡(Sn)、Sn-M(其中M是G2-G7原子)、TmSby(其中Tm是过渡金属)、铋(Bi)、银(Ag)、铝(Al)和锌(Zn)。在这些情况下,第一阳极层24的第二材料29将相应地是(其中AM表示碱金属)、Sn-AM合金、Sn-M-AM合金(其中M是G2-G7原子)、TmSby-AM合金(其中Tm是过渡金属)、Bi-AM合金、Ag-AM合金、Al-AM合金或Zn-AM合金。Particularly preferred materials that may be particularly suitable for lithium-ion batteries include, for example: tin (Sn), Sn-M (wherein M is a G2-G7 atom), TmSby (wherein Tm is a transition metal), bismuth (Bi), silver ( Ag), aluminum (Al) and zinc (Zn). In these cases, the second material 29 of the first anode layer 24 will accordingly be (wherein AM represents an alkali metal), a Sn-AM alloy, a Sn-M-AM alloy (wherein M is a G2-G7 atom), TmSb y - AM alloys (where Tm is a transition metal), Bi-AM alloys, Ag-AM alloys, Al-AM alloys or Zn-AM alloys.
第一阳极层将具有由第一阳极材料和/或第一阳极层的厚度确定的第一碱金属离子存量I1的容量。当第一阳极层完全合金化,使得它被碱金属离子饱和,并且已经形成第二阳极材料时,该存量I1将完全容纳在第一阳极层中。The first anodic layer will have a capacity of a first alkali metal ion inventory I 1 determined by the first anode material and/or the thickness of the first anodic layer. When the first anode layer is fully alloyed so that it is saturated with alkali metal ions, and the second anode material has been formed, this inventory I1 will be completely contained in the first anode layer.
优选地选择第一阳极材料,使得其与碱金属形成具有相对低的碱金属存量I1的合金,即,当合金被碱金属饱和时,其具有相对低的碱金属含量A2。选择相对较低的碱金属存量意味着在第二阳极材料的合金中包含相对较少的碱金属,并且更多的碱金属可以用于在第一阳极层24和阳极集流体层22之间的边界30处电镀碱金属。通过确保大量的碱金属可以用于电镀机制,电池的容量可以最大化。The first anode material is preferably chosen such that it forms an alloy with the alkali metal having a relatively low alkali metal inventory I 1 , ie it has a relatively low alkali metal content A 2 when the alloy is saturated with the alkali metal. Selecting a relatively low alkali metal inventory means that relatively less alkali metal is included in the alloy of the second anode material and more alkali metal is available for the Alkali metal is plated at the boundary 30 . By ensuring that a large amount of alkali metal is available for the plating mechanism, the capacity of the battery can be maximized.
当阳极14结合到具有阴极12的电池10中时,如图1和2所示,阴极将具有由阴极材料和/或阴极层厚度确定的第二碱金属离子存量I2。优选具体地选择第一阳极层的参数(具体地,第一阳极材料和第一阳极层的厚度),使得I1≤0.5I2。这意味着当阴极的存量被放电50%或更少时,第一阳极层将被碱金属离子饱和。然后,阴极12的剩余存量(I2-I1)将作为纯碱金属容纳在第二阳极层26中。When an
尽管相对低的碱金属存量I1对于第一阳极层24是期望的,但是应当注意,因为第二阳极材料29是碱金属和第一合金材料26的合金混合物(而不是例如一些少量碱金属离子可能扩散通过的非合金材料),所以合金的碱金属含量将仍然足够高以构成合金。例如,第二阳极材料的碱金属离子含量可以至少为10at%,优选至少为20at%。Although a relatively low alkali metal inventory I is desirable for the first anode layer 24, it should be noted that since the second anode material 29 is an alloy mixture of an alkali metal and the first alloy material 26 (rather than, for example, some small amount of alkali metal ions non-alloyed materials that may diffuse through), so the alkali metal content of the alloy will still be high enough to form the alloy. For example, the alkali metal ion content of the second anode material may be at least 10 at%, preferably at least 20 at%.
第一材料优选通过物理气相沉积直接沉积到固体电解质上。The first material is deposited directly onto the solid electrolyte, preferably by physical vapor deposition.
第一材料层的厚度根据电池的要求定制,并且可以受到包括如上所述的阴极存量的因素的影响,并且还受到电解质的材料和第一阳极材料的选择的影响。根据电极和电极并入其中的电池的参数和材料,典型的厚度将例如在大约5纳米和大约100微米之间。通常,希望第一材料层尽可能薄。特别优选的厚度是能够提供阴极锂存量的大约20%的过剩容量的厚度。The thickness of the first material layer is tailored to the requirements of the battery and can be influenced by factors including the cathode inventory as described above, and also by the choice of electrolyte and first anode material. Typical thicknesses will, for example, be between about 5 nanometers and about 100 micrometers, depending on the parameters and materials of the electrodes and the battery into which they are incorporated. In general, it is desirable that the first layer of material is as thin as possible. A particularly preferred thickness is one capable of providing an excess capacity of about 20% of the lithium inventory of the cathode.
选择阳极集流体层的材料,使其能够抵抗与碱金属形成合金,并且能够抵抗碱金属通过该层的扩散。这确保了碱金属将被镀在第一阳极层和集流体层之间的边界处,而不是与集流体层合金化或扩散通过集流体层,否则这将允许碱金属离子逸出,耗尽电池的容量。阳极集流体层的材料也被选择为导电的。The material of the anode current collector layer is chosen to be resistant to alloying with alkali metals and to resist diffusion of alkali metals through the layer. This ensures that the alkali metal will be plated at the boundary between the first anode layer and the current collector layer, rather than alloyed with or diffused through the current collector layer, which would otherwise allow alkali metal ions to escape, depleting the The capacity of the battery. The material of the anode current collector layer is also selected to be conductive.
用于阳极集流体的合适材料包括抵抗与电池的碱金属离子合金化的过渡金属:例如铜(Cu)、铂(Pt)、镍(Ni)、钼(Mo)和钨(W)。Suitable materials for the anode current collector include transition metals that resist alloying with the cell's alkali metal ions: eg copper (Cu), platinum (Pt), nickel (Ni), molybdenum (Mo) and tungsten (W).
固体电解质可以是能够承载碱金属离子的任何合适的材料。例如,当电池的碱金属是锂时,固体电解质可以是LiPON。The solid electrolyte can be any suitable material capable of supporting alkali metal ions. For example, when the alkali metal of the battery is lithium, the solid electrolyte may be LiPON.
阳极可以使用现在将参考图3a至3c描述的物理气相沉积(PVD)方法来制造。The anode can be fabricated using the physical vapor deposition (PVD) method which will now be described with reference to Figures 3a to 3c.
优选地,阳极14被制成图1所示的未充电状态。使阳极14处于未充电状态是特别有利的,因为在这种状态下,阳极14基本上不含高活性碱金属,使得其易于制造和处理。不需要沉积任何纯碱金属层,这有利于制造。Preferably, the
如图3a所示,首先提供固体电解质16。在图3a的示例中,固体电解质16是还包括阴极层和阴极集流体的结构的顶层。固体电解质16限定了随后将在其上沉积阳极14的基底。As shown in Figure 3a, a
接下来,如图3n所示,将包括第一阳极材料26的第一阳极层24沉积到固体电解质16上。使用PVD方法沉积材料,例如溅射。因此,固体电极16在沉积之前布置在溅射设备的真空室中。Next, as shown in FIG. 3 n , a first anode layer 24 comprising a first anode material 26 is deposited onto the
在第一阳极层24就位的情况下,阳极集流体层22沉积在第一阳极层24上。第一阳极集流体层22也使用PVD方法沉积,例如溅射。With the first anode layer 24 in place, the anode
在该示例中,不需要在阳极集流体层22之前沉积任何另外的阳极层。特别地,不需要沉积包含碱金属的第二阳极层,因为该层可以在随后的充电过程中形成。In this example, there is no need to deposit any additional anode layer prior to the anode
在阳极集流体层22就位的情况下,阳极14在其未充电状态下是完整的,并且可以从沉积设备中移除。然后阳极准备好在电池中使用,在电池中它可以根据上述机制充电和放电。With the anode
所描述的阳极结构提供了高能量密度的电池,其可以专门在放电状态下制造,从而允许安全和容易地制造。因为主要的阳极充电机制是碱金属的电镀,所以电池具有高容量。在沉积的集流体层下电镀碱金属意味着碱金属不会从电池中损失,并且容量得以保持。合金材料的存在意味着锂电镀以低速率发生,促进均匀电镀并减少枝晶生长,否则枝晶生长会有碍电池容量。The described anode structure provides a high energy density battery that can be fabricated exclusively in the discharged state, allowing safe and easy fabrication. Because the primary anode charging mechanism is the plating of alkali metals, the battery has a high capacity. Electroplating the alkali metal under the deposited current collector layer means that the alkali metal is not lost from the battery and the capacity is maintained. The presence of the alloy material means that lithium plating occurs at a low rate, promoting uniform plating and reducing dendrite growth, which would otherwise hinder battery capacity.
现在将参照图4、5、6和7a至7d描述本发明的另一个实施例。Another embodiment of the invention will now be described with reference to Figures 4, 5, 6 and 7a to 7d.
图4和5示出了类似于图1和2的阳极14的阳极114,除了i)包括碱金属的第二阳极层128以充电和放电两种状态存在,以及ii)第一合金层124包括处于充电和放电两种状态的第二材料129。在该实施例中,第二阳极层128在充电状态下的总体积以及因此的总厚度大于在放电状态下。Figures 4 and 5 show an
参照示出放电状态的图4,在放电状态下,阳极114包括邻近电解质116的第一阳极层124和位于第一阳极层124和阳极集流体层122之间的第二阳极层128。在该实施例中,第一阳极层124包括第二材料129,第二材料129是包括电池的碱金属的合金,具有碱金属离子含量A2。第二阳极层128包括碱金属,并且具有第一厚度t1。Referring to FIG. 4 illustrating a discharged state, in the discharged state, the
在图5所示的充电状态下,阳极114包括与电解质116相邻的第一阳极层124和位于第一阳极层124和阳极集流体层122之间的第二阳极层128。在该充电状态下,第一阳极层124还包括第二材料129。第二阳极层128包括碱金属,并且具有大于第一厚度t1的第二厚度t2。In the state of charge shown in FIG. 5 , the
与图1和图2的阳极一样,图4和图5的阳极可以在放电状态下制造。然而,在这种情况下,阳极不是精确地以图4的放电状态制造的,而是以图6所示的替代的放电状态制造的。该状态基本上与图4的放电状态相同,除了第一阳极层124包括与图1的实施例相同类型的第一材料126,即能够与碱金属离子合金化的材料,并且具有小于A2的碱金属离子含量A1,在这种情况下,A1基本上为0。Like the anodes of Figures 1 and 2, the anodes of Figures 4 and 5 can be fabricated in a discharged state. In this case, however, the anode is not produced in exactly the discharge state of FIG. 4 , but in an alternative discharge state shown in FIG. 6 . This state is substantially the same as the discharge state of FIG. 4, except that the first anode layer 124 comprises the same type of first material 126 as in the embodiment of FIG . Alkali metal ion content A 1 , in this case A 1 is essentially zero.
制造后电池第一次充电时,阳极从图6的替代放电状态充电到图5的充电状态。阳极经历与图1和图2的阳极相同的两种阳极充电机制:合金化机制和电镀机制。合金化机制与上述基本相同。碱金属电镀机制与上述类似,但是在这种情况下,一些碱金属已经存在于第一阳极层124和集流体层122之间的第二阳极层128中。在这种情况下,当在充电期间“电镀”碱金属时,第二阳极层128的碱金属的厚度从未充电厚度t1增加到充电厚度t2。以这种方式,借助于电镀机制,碱金属的总体积以及因此第二阳极层128的总体积在充电期间增加。When the battery is charged for the first time after manufacture, the anode is charged from the alternate discharge state of FIG. 6 to the charge state of FIG. 5 . The anode undergoes the same two anodic charging mechanisms as the anodes of Figures 1 and 2: the alloying mechanism and the plating mechanism. The alloying mechanism is basically the same as above. The alkali metal plating mechanism is similar to that described above, but in this case some alkali metal is already present in the
在第一个(以及所有后续)放电循环期间,阳极从图5的充电状态放电到图4的放电状态。将发生去电镀机制,通过该去电镀机制,第二阳极层128的至少一些碱金属经由合金化机制通过第一阳极层124扩散回到固体电解质116,使得第二阳极层的厚度从t2减小到t1。在该实施例中,放电循环不涉及第一阳极层124的去合金化。During the first (and all subsequent) discharge cycles, the anode is discharged from the charged state of FIG. 5 to the discharged state of FIG. 4 . A deplating mechanism will occur by which at least some of the alkali metal of the
在随后的充电周期中,阳极从图4的放电状态充电到图5的充电状态。在该充电循环中,阳极不经历合金化机制,而仅经历上述碱金属电镀机制,其中第二阳极层128的碱金属厚度从未充电厚度t1增加到充电厚度t2。During the subsequent charging cycle, the anode is charged from the discharged state of FIG. 4 to the charged state of FIG. 5 . During this charge cycle, the anode does not undergo an alloying mechanism, but only an alkali metal plating mechanism as described above, wherein the alkali metal thickness of the
随后的充电和放电循环如上所述继续,阳极在图4的放电状态和图5的充电状态之间充电和放电。由于第一阳极层124没有经历去合金化,阳极没有返回到图6的替代放电状态。Subsequent charge and discharge cycles continue as described above, with the anode charging and discharging between the discharge state of FIG. 4 and the charge state of FIG. 5 . Since the first anode layer 124 has not undergone dealloying, the anode does not return to the alternate discharge state of FIG. 6 .
图7a至7d示出了制造图6所示阳极的各个阶段。该工艺通常类似于结合图3a至3c描述的工艺,除了在附加步骤中沉积碱金属层。7a to 7d show various stages in the manufacture of the anode shown in FIG. 6 . The process is generally similar to that described in connection with Figures 3a to 3c, except that the alkali metal layer is deposited in an additional step.
如图7a所示,首先提供固体电解质116。在图7a的示例中,固体电解质116是还包括阴极层和阴极集流体的结构的顶层。固体电解质116限定了随后将在其上沉积阳极114的基底。As shown in Figure 7a, a
接下来,如图7b所示,将包括第一阳极材料126的第一阳极层124沉积到固体电解质116上。使用PVD方法沉积材料,例如溅射。因此,固体电极116在沉积之前布置在溅射设备的真空室中。Next, as shown in FIG. 7 b , a first anode layer 124 comprising a first anode material 126 is deposited onto the
在第一阳极层124就位的情况下,如图7c所示,包括碱金属的第二阳极层128沉积在第一阳极层124的顶部,也使用PVD方法,例如溅射。With the first anode layer 124 in place, as shown in Figure 7c, a
接下来,如图7d所示,在第二阳极层128上沉积阳极集流体层122。阳极集流体层122也使用PVD方法沉积,例如溅射。Next, as shown in FIG. 7 d , an anode
在阳极集流体层122就位的情况下,阳极在其替代放电状态下是完整的,并且可以从沉积设备中移除。然后阳极准备好在电池中使用,在电池中它可以根据上述机制充电和放电。With the anode
应当理解,子层可以存在于上述任何阳极层中。例如,第一阳极层可以包括不同材料的子层,其中一些或所有子层可以与碱金属合金化。It should be understood that sublayers may be present in any of the anode layers described above. For example, the first anode layer may comprise sublayers of different materials, some or all of which may be alloyed with an alkali metal.
在上面的示例中,已经描述了处于完全充电和完全放电状态的阳极结构。然而,应当理解,阳极结构也可以以部分充电状态存在。还应理解,由于电池内的寄生反应和动力学限制,在实践中,电池可能无法实现完全的充电和放电状态。例如,在第一实施例中,脱合金可能不完全,使得在放电状态下,少量碱金属离子可能残留在第一阳极层中,例如使得A1可能不是0,而是可能是诸如≤1at%的较小值。去电镀也可能是不完全的,使得少量的第二阳极层存在于放电状态。In the examples above, the anode structure has been described in fully charged and fully discharged states. However, it should be understood that the anode structure may also exist in a partially charged state. It should also be understood that, in practice, a battery may not be able to achieve full states of charge and discharge due to parasitic reactions and kinetic limitations within the battery. For example, in the first embodiment, dealloying may not be complete, so that in the discharged state, a small amount of alkali metal ions may remain in the first anode layer, such that A1 may not be 0, but may be such as ≤ 1 at % smaller value of . Deplating may also be incomplete such that a small amount of the second anode layer exists in a discharged state.
在不脱离所附权利要求的范围的情况下,其他变化对于技术人员来说是显而易见的。Other variations will be apparent to the skilled person without departing from the scope of the appended claims.
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| US20190157723A1 (en) * | 2017-11-21 | 2019-05-23 | Samsung Electronics Co., Ltd. | All-solid-state secondary battery and method of charging the same |
| US20200152986A1 (en) * | 2018-11-14 | 2020-05-14 | Samsung Electronics Co., Ltd. | All-solid secondary battery and method of manufacturing the same |
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| JP6597701B2 (en) * | 2017-04-18 | 2019-10-30 | トヨタ自動車株式会社 | Negative electrode mixture, negative electrode including the negative electrode mixture, and all-solid-state lithium ion secondary battery including the negative electrode |
| JP6776995B2 (en) * | 2017-04-18 | 2020-10-28 | トヨタ自動車株式会社 | Manufacturing method of all-solid-state lithium-ion secondary battery |
| JP7034704B2 (en) * | 2017-12-22 | 2022-03-14 | 昭和電工株式会社 | Manufacturing method of lithium ion secondary battery |
| US12080880B2 (en) * | 2018-09-25 | 2024-09-03 | Toyota Motor Engineering & Manufacturing North America, Inc. | Nano-alloy interphase for lithium metal solid state batteries |
| KR102682128B1 (en) * | 2018-11-07 | 2024-07-08 | 삼성전자주식회사 | Anodeless coating layer for All-solid-state battery and All-solid-state battery including the same |
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| US20190157723A1 (en) * | 2017-11-21 | 2019-05-23 | Samsung Electronics Co., Ltd. | All-solid-state secondary battery and method of charging the same |
| CN108232320A (en) * | 2018-02-08 | 2018-06-29 | 天津瑞晟晖能科技有限公司 | The preparation method and solid-State Thin Film Li-Ion Batteries of solid-State Thin Film Li-Ion Batteries |
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