CN105655646A - Lithium ion energy storage element and manufacturing method thereof - Google Patents
Lithium ion energy storage element and manufacturing method thereof Download PDFInfo
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Abstract
本发明提供一种锂离子储能元件,其包括正极,正极包含第一集电片及位于第一集电片上的正极活性物质;负极,其包含第二集电片及位于第二集电片上的负极活性物质,负极活性物质系选自由含碳材料、Si合金及Sn合金所组成的族群;以及电解质,其中正极活性物质包含锂离子提供者及正极框架活性物质,该锂离子提供者为过氧化锂、氧化锂或两者的混合物。本发明亦有关一种锂离子储能元件的制造方法。
The present invention provides a lithium ion energy storage element, which includes a positive electrode, the positive electrode includes a first collector and a positive electrode active material located on the first collector; a negative electrode, which includes a second collector and a negative electrode active material located on the second collector, the negative electrode active material is selected from the group consisting of carbonaceous materials, Si alloys and Sn alloys; and an electrolyte, wherein the positive electrode active material includes a lithium ion provider and a positive electrode frame active material, the lithium ion provider is lithium peroxide, lithium oxide or a mixture of the two. The present invention also relates to a method for manufacturing a lithium ion energy storage element.
Description
技术领域 technical field
本发明与锂离子储能元件有关,特别有关于正极活性物质包含锂离子提供者及正极框架活性物质的锂离子储能元件。 The invention relates to a lithium ion energy storage element, in particular to a lithium ion energy storage element whose anode active material includes a lithium ion provider and an anode frame active material.
背景技术 Background technique
在众多的储能技术中,锂离子电池由于具有能量密度大、循环寿命长、重量轻、无污染等优点,被认为是下一代高效可携式化学电源。目前已经广泛的用于数码相机、智能手机、笔记本电脑等方面。随着锂离子电池能量密度的进一步提升,其应用领域扩大。随着可移动电子设备对高容量、长寿命电池需求的日益增长,人们对锂离子电池的性能提出了更高的要求。 Among numerous energy storage technologies, lithium-ion batteries are considered to be the next generation of high-efficiency portable chemical power sources due to their high energy density, long cycle life, light weight, and non-pollution. At present, it has been widely used in digital cameras, smart phones, notebook computers and so on. With the further improvement of the energy density of lithium-ion batteries, its application fields have expanded. With the increasing demand for high-capacity, long-life batteries for mobile electronic devices, people have put forward higher requirements for the performance of lithium-ion batteries.
锂离子电池通常包含负极、电解质及正极。锂离子电池的正极活性物质不仅作为电极材料参与电化学反应,而且可作为锂源,正极活性物质通常是含有锂原子嵌入其中的锂金属氧化物。目前市场上常用的锂金属氧化物为钴酸锂、镍酸锂及锰酸锂等。然而,上述锂金属氧化物于重复充放电后,无一能展示高起始电容量、高热稳定性及好的电容量维持性的适当组合特性。 Lithium-ion batteries generally include a negative electrode, an electrolyte, and a positive electrode. The positive active material of a lithium-ion battery not only participates in the electrochemical reaction as an electrode material, but also serves as a lithium source. The positive active material is usually a lithium metal oxide containing lithium atoms embedded in it. Lithium metal oxides commonly used in the market are lithium cobalt oxide, lithium nickel oxide, and lithium manganese oxide. However, none of the aforementioned lithium metal oxides can exhibit the proper combination of high initial capacity, high thermal stability, and good capacity retention after repeated charge-discharge.
锂离子电池受限于其正极锂金属氧化物的单位电容量,而无法展示高的单位电容量。因此,如果要提高锂电池的单位电容量,必需增加锂的来源。一般作法以锂金属作为锂源均匀的涂布于负极,或以第三极的方式电镀于负极,由于锂金属非常的活泼,以上两种工法非常困难不容易执行,同时也不容易均匀分布。 Lithium-ion batteries are limited by the specific capacity of their cathode lithium metal oxides, and cannot exhibit high specific capacity. Therefore, if the unit capacity of the lithium battery is to be increased, the source of lithium must be increased. Generally, lithium metal is used as the lithium source to evenly coat the negative electrode, or to be electroplated on the negative electrode as the third electrode. Since lithium metal is very active, the above two methods are very difficult and difficult to implement, and it is also not easy to distribute evenly.
由于锂金属有安全性及稳定性等缺点,因此目前商业化的锂离子二次电池只能使用含有锂离子的正极材料与可储存锂离子的负极材料作为工作系统。由于近年来,能源需求快速提升,锂离子二次电池的能量密度势必得再提升,尤其正极材料可说是整个电池的核心。然而,受限于正极材料结构上的稳定性及锂离子的可嵌出量,克电容量的提升已达瓶颈。 Due to the disadvantages of lithium metal such as safety and stability, current commercialized lithium-ion secondary batteries can only use positive electrode materials containing lithium ions and negative electrode materials that can store lithium ions as the working system. Due to the rapid increase in energy demand in recent years, the energy density of lithium-ion secondary batteries is bound to be further improved, especially the cathode material can be said to be the core of the entire battery. However, limited by the structural stability of the positive electrode material and the amount of lithium ions that can be intercalated, the increase in gram capacity has reached a bottleneck.
有人提出一些材料例如FeF3、FePO4及V2O5等,它们具有良好的电容量及较高的平台电压,是提升能量密度的候选材料。然而却碍于本身不含锂离子而须与锂金属搭配,只适用于半电池测试,无法使用于全电池中,限制了正极材料的选择性。 It has been proposed that some materials such as FeF 3 , FePO 4 and V 2 O 5 have good capacitance and high plateau voltage and are candidate materials for increasing energy density. However, due to the fact that it does not contain lithium ions, it must be matched with lithium metal. It is only suitable for half-cell testing and cannot be used in full batteries, which limits the selectivity of positive electrode materials.
发明内容 Contents of the invention
为了解决上述技术问题,本发明提供一种锂离子储能元件,借由使用包含锂离子提供者及正极框架活性物质的正极活性物质,可展示高的单位电容量。 In order to solve the above technical problems, the present invention provides a lithium ion energy storage element, which can exhibit high unit capacity by using a positive electrode active material including a lithium ion provider and a positive electrode frame active material.
本发明提供的一种锂离子储能元件,包括: A lithium ion energy storage element provided by the present invention comprises:
一正极,其包含一第一集电片及位于该第一集电片上的正极活性物质; A positive electrode, which includes a first current collector and a positive active material on the first current collector;
一负极,其包含一第二集电片及位于该第二集电片上的一负极活性物质,该负极活性物质选自由一含碳材料、Si合金及Sn合金所组成的族群;及 A negative electrode comprising a second current collector and a negative active material on the second current collector, the negative active material is selected from the group consisting of a carbonaceous material, Si alloy and Sn alloy; and
一电解质,位于该正极与该负极之间,其中该正极活性物质包含一锂离子提供者及一正极框架活性物质,该锂离子提供者为过氧化锂、氧化锂或两者的混合物。 An electrolyte, located between the positive electrode and the negative electrode, wherein the positive active material includes a lithium ion provider and a positive frame active material, the lithium ion provider is lithium peroxide, lithium oxide or a mixture of both.
优选地,该正极活性物质的该正极框架活性物质选自由锐钛矿相二氧化钛、碳硫复合物、含碳材料及氟碳材料所组成的族群。 Preferably, the positive frame active material of the positive active material is selected from the group consisting of anatase titanium dioxide, carbon-sulfur composites, carbonaceous materials and fluorocarbon materials.
优选地,该正极框架活性物质的碳硫复合物的硫碳比例为5~7:3~5。 Preferably, the ratio of sulfur to carbon in the carbon-sulfur composite of the positive frame active material is 5-7:3-5.
优选地,该正极框架活性物质是锂金属氧化物。 Preferably, the positive frame active material is lithium metal oxide.
优选地,该正极活性物质更包含一导电碳,该导电碳为superP碳黑、KS6石墨或两者的组合。 Preferably, the positive active material further includes a conductive carbon, and the conductive carbon is superP carbon black, KS6 graphite or a combination of both.
本发明还提供一种锂离子储能元件的制造方法,包含以下步骤: The present invention also provides a manufacturing method of a lithium ion energy storage element, comprising the following steps:
(a)将锂离子提供者、正极框架活性物质及粘着剂分别以一定的重量比混合,并将其加入于一分散剂中而制备正极活性物质,其中该锂离子提供者为过氧化锂、氧化锂或两者的混合物; (a) Mix the lithium ion provider, the positive electrode frame active material and the binder respectively in a certain weight ratio, and add them to a dispersant to prepare the positive electrode active material, wherein the lithium ion provider is lithium peroxide, Lithium oxide or a mixture of both;
(b)将该正极活性物质涂布到一铝箔成膜后,将涂布好的电极烘干,由此制备正极;及 (b) After coating the positive electrode active material on an aluminum foil to form a film, drying the coated electrode to prepare the positive electrode; and
(c)使用该制备所得的正极、具有负极活性物质的负极及夹置于其中的一多孔性隔离膜,将电解质注入该正极和该负极之间,由此制作一锂离子储能元件。 (c) Using the prepared positive electrode, the negative electrode with the negative active material and a porous separator interposed therein, injecting electrolyte between the positive electrode and the negative electrode, thereby fabricating a lithium ion energy storage element.
优选地上述的锂离子储能元件的制造方法,更包含于注入电解质之后的首圈充放电所产生的氧气去除步骤。 Preferably, the above-mentioned manufacturing method of the lithium-ion energy storage element further includes a step of removing oxygen generated in the first cycle of charging and discharging after the electrolyte is injected.
优选地,步骤(a)的正极框架活性物质选自由锐钛矿相二氧化钛、碳硫复合物、含碳材料及氟碳材料所组成的族群。 Preferably, the positive frame active material in step (a) is selected from the group consisting of anatase phase titanium dioxide, carbon-sulfur composites, carbonaceous materials and fluorocarbon materials.
优选地,步骤(a)的正极框架活性物质锂金属氧化物。 Preferably, the positive electrode frame active material in step (a) is lithium metal oxide.
优选地,步骤(a)更添加一导电碳以制作该正极活性物质,该导电碳为superP碳黑、KS6石墨或两者的组合。 Preferably, step (a) further adds a conductive carbon to make the positive electrode active material, and the conductive carbon is superP carbon black, KS6 graphite or a combination of both.
优选地,步骤(a)的粘着剂为聚偏氟乙烯或羧甲基纤维素。 Preferably, the adhesive in step (a) is polyvinylidene fluoride or carboxymethyl cellulose.
优选地,步骤(c)的负极活性物质选自由石墨化中间相碳微球、硬碳、Si合金及Sn合金所组成的族群。 Preferably, the negative electrode active material in step (c) is selected from the group consisting of graphitized mesocarbon microspheres, hard carbon, Si alloy and Sn alloy.
优选地,步骤(c)的电解质为在碳酸亚乙酯和碳酸二乙酯的混合体积比为1:1的混合溶液中溶解有1M浓度的LiPF6,或是在四乙二醇二甲醚和1,3-二氧戊烷的混合体积比为1:1的混合溶液中溶解有1M浓度的双三氟甲基磺酸亚酰胺锂。 Preferably, the electrolyte in step (c) is LiPF 6 with a concentration of 1M dissolved in a mixed solution of ethylene carbonate and diethyl carbonate with a mixing volume ratio of 1:1, or in tetraethylene glycol dimethyl ether Lithium bistrifluoromethanesulfonate imide at a concentration of 1M was dissolved in a mixed solution having a mixing volume ratio of 1:1 with 1,3-dioxolane.
优选地,步骤(a)的分散剂为N-甲基-2-吡咯烷酮。 Preferably, the dispersant in step (a) is N-methyl-2-pyrrolidone.
具体地,本发明的锂离子储能元件的制造方法,首先将过氧化锂;正极框架活性物质,例如二氧化钛;及粘着剂,例如聚偏氟乙烯(PVDF)以一定的重量比混合,并将其分散于N-甲基-2-吡咯烷酮而得到浆料。然后将上述浆料倒在铝箔上,使用刮刀涂布机将浆料涂布成膜。将涂布好的的电极置入在80~90°c的烘箱中去除溶剂,然后升温至120~130°c烘干一段时间,由此制备过氧化锂/二氧化钛极片。为了增加过氧化锂的导电度,可添加导电碳,例如superP碳黑、KS6石墨或两者的组合。 Specifically, in the manufacturing method of the lithium ion energy storage element of the present invention, first, lithium peroxide; positive electrode frame active material, such as titanium dioxide; and binder, such as polyvinylidene fluoride (PVDF) are mixed in a certain weight ratio, and It is dispersed in N-methyl-2-pyrrolidone to give a slurry. Then the above slurry was poured on the aluminum foil, and the slurry was coated into a film using a knife coater. Place the coated electrode in an oven at 80-90°C to remove the solvent, then heat up to 120-130°C and dry for a period of time, thereby preparing lithium peroxide/titanium dioxide pole pieces. To increase the conductivity of lithium peroxide, conductive carbon such as superP carbon black, KS6 graphite or a combination of both can be added.
使用上述制备的过氧化锂/二氧化钛极片、作为负极的石墨化中间相碳微球(MCMB)及多孔性隔离膜,将在碳酸亚乙酯(EC)和碳酸二乙酯(DEC)的混合体积比为1:1的混合溶液中溶解有1M浓度的LiPF6的电解质,注入上述过氧化锂极片和负极之间,由此制作全电池。 Using the lithium peroxide/titanium dioxide pole piece prepared above, the graphitized mesocarbon microspheres (MCMB) as the negative electrode and the porous separator, the mixture of ethylene carbonate (EC) and diethyl carbonate (DEC) An electrolyte with 1M concentration of LiPF6 dissolved in a mixed solution with a volume ratio of 1:1 was injected between the above-mentioned lithium peroxide pole piece and the negative electrode, thereby producing a full battery.
本发明的另一种锂离子储能元件的制造方法,首先将过氧化锂;正极框架活性物质,例如碳硫复合物;及粘着剂例如羧甲基纤维素(CMC)以一定的重量比混合,并将其分散于N-甲基-2-吡咯烷酮而得到浆料。然后将上述浆料倒在铝箔上,使用刮刀涂布机将浆料涂布成膜。将涂布好的的电极置入在80~90°c的烘箱中去除溶剂,然后升温至120~130°c烘干一段时间,由此制备过氧化锂/碳硫复合物极片。为了增加过氧化锂的导电度,可添加导电碳,例如superP碳黑、KS6石墨或两者的组合。 Another manufacturing method of lithium ion energy storage element of the present invention, at first with lithium peroxide; Positive frame active material, such as carbon-sulfur compound; And binding agent such as carboxymethylcellulose (CMC) is mixed with certain weight ratio , and disperse it in N-methyl-2-pyrrolidone to obtain a slurry. Then the above slurry was poured on the aluminum foil, and the slurry was coated into a film using a knife coater. Place the coated electrode in an oven at 80-90°C to remove the solvent, then heat up to 120-130°C and dry for a period of time, thereby preparing a lithium peroxide/carbon-sulfur composite pole piece. To increase the conductivity of lithium peroxide, conductive carbon such as superP carbon black, KS6 graphite or a combination of both can be added.
使用上述制备的过氧化锂/碳硫复合物极片、作为负极的硬碳及多孔性隔离膜,将在四乙二醇二甲醚(TEGDME)和1,3-二氧戊烷(DOL)的混合体积比为1:1的混合溶液中溶解有1M浓度的双三氟甲基磺酸亚酰胺锂的电解质,注入上述过氧化锂极片和负极之间,由此制作全电池。 Use the above-mentioned lithium peroxide/carbon-sulfur composite pole sheet prepared above, as the hard carbon of the negative pole and the porous separator, will be in tetraethylene glycol dimethyl ether (TEGDME) and 1,3-dioxolane (DOL) An electrolyte in which lithium bistrifluoromethanesulfonate imide at a concentration of 1M is dissolved in a mixed solution with a mixing volume ratio of 1:1 is injected between the lithium peroxide pole piece and the negative electrode, thereby producing a full battery.
相较于现有含有锂金属氧化物的锂离子电池,本发明的锂离子储能元件,藉由使用含有过氧化锂及正极框架活性物质的正极活性物质,利用电化学充电的方式将过氧化锂及/或氧化锂分解,产生锂离子,之后便可在正极框架活性物质、负极活性物质的全电池中反复的嵌入与嵌出,可展示高的单位电容量。 Compared with the existing lithium-ion batteries containing lithium metal oxides, the lithium-ion energy storage element of the present invention uses a positive electrode active material containing lithium peroxide and a positive electrode frame active material to electrochemically charge the peroxide Lithium and/or lithium oxide are decomposed to generate lithium ions, which can then be repeatedly intercalated and intercalated in the full battery of positive electrode frame active material and negative electrode active material, and can exhibit high unit capacity.
附图说明 Description of drawings
图1显示根据本发明的一实施例的锂离子电池的单元电池结构。 FIG. 1 shows a unit cell structure of a lithium ion battery according to an embodiment of the present invention.
图2为本发明过氧化锂的半电池充放电的电压对电容量的第1循环曲线图。 Fig. 2 is the first cycle graph of the voltage versus the capacity of the lithium peroxide half-cell charge and discharge of the present invention.
图3为本发明过氧化锂的半电池充放电的电压对电容量的第2和3循环曲线图。 Fig. 3 is the 2nd and 3rd cycle graphs of the voltage versus the capacity of the lithium peroxide half-cell charge and discharge of the present invention.
图4是本发明过氧化锂于不同导电碳比例下的半电池充放电的电压对电容量的第1循环曲线图。 Fig. 4 is the first cycle graph of the voltage versus capacity of half-cell charging and discharging of lithium peroxide of the present invention under different conductive carbon ratios.
图5是过氧化锂和导电碳不同比例下的循环电位扫描。 Figure 5 is a cycle potential scan at different ratios of lithium peroxide and conductive carbon.
图6是显示不同电流密度对于过氧化锂的电压对电容量的影响。 Figure 6 shows the effect of different current densities on the voltage of lithium peroxide on the capacity.
图7为过氧化锂/二氧化钛对Li/Li+的半电池预置锂充放电曲线。 Figure 7 is the half-cell preset lithium charge and discharge curve of lithium peroxide/titanium dioxide on Li/Li+.
图8为预置锂阶段后的二氧化钛的充放电曲线。 Fig. 8 is the charging and discharging curve of titanium dioxide after the lithium stage is preset.
图9为过氧化锂/二氧化钛对石墨化中间相碳微球(MCMB)的全电池预置锂充放电曲线。 Figure 9 is the preset lithium charge and discharge curves of the full battery of lithium peroxide/titanium dioxide on graphitized mesocarbon microspheres (MCMB).
图10为预置锂阶段后的二氧化钛的充放电曲线。 Fig. 10 is the charging and discharging curve of titanium dioxide after the lithium stage is preset.
图11显示具有去除氧气的过氧化锂/二氧化钛对石墨化中间相碳微球(MCMB)的全电池预置锂充放电曲线。 Figure 11 shows the full-cell preset lithium charge-discharge curves of graphitized mesocarbon microspheres (MCMB) with lithium peroxide/titanium dioxide with oxygen removal.
图12为具有去除氧气的预置锂阶段后的二氧化钛的充放电曲线。 Figure 12 is the charge-discharge curve of titanium dioxide after a pre-lithium stage with oxygen removal.
图13显示过氧化锂在醚类电解质中相对于锂金属于2~4.3V进行的半电池的充放电曲线。 Figure 13 shows the charge-discharge curves of a half-cell of lithium peroxide in an ether electrolyte versus lithium metal at 2-4.3V.
图14显示碳硫复合物电极组成半电池的充放电曲线。 Figure 14 shows the charge-discharge curves of the half-cell composed of carbon-sulfur composite electrodes.
图15过氧化锂/碳硫复合物对Li/Li+的半电池预置锂充放电曲线。 Figure 15 Lithium peroxide/carbon-sulfur composites for Li/Li + half-cell preset lithium charge-discharge curves.
附图标记说明: Explanation of reference signs:
100单元电池结构; 100 cell battery structure;
104多孔性隔离膜; 104 porous isolation membrane;
106正极; 106 positive pole;
105黏着剂; 105 adhesives;
108负极; 108 negative pole;
110第一集电片; 110 The first episode;
112第二集电片; 112 second collector sheet;
114正极活性物质; 114 positive active material;
116负极活性物质。 116 negative active material.
具体实施方式 detailed description
下面结合附图和具体实施例对本发明作进一步说明,以使本领域的技术人员可以更好的理解本发明并能予以实施,但所举实施例不作为对本发明的限定。 The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments, so that those skilled in the art can better understand the present invention and implement it, but the examples given are not intended to limit the present invention.
图1显示根据本发明的一实施例的锂离子储能元件的单元电池结构。本实施例的锂离子储能元件包含多个单元电池结构100,每一单元电池结构100包含多孔性隔离膜104夹置在正极106及负极108之间。多孔性隔离膜104涂布粘着剂105增加电池结构100的元件彼此之间的连接性。正极106包含第一集电片110及位于第一集电片110上的正极活性物质114,及负极108包含第二集电片112及位于第二集电片112上的负极活性物质116。正极活性物质114包含锂离子提供者及正极框架活性物质,其中锂离子提供者可为过氧化锂,正极框架活性物质例如锐钛矿相二氧化钛或碳硫复合物。碳硫复合物中硫碳比例为5~7:3~5。过氧化锂/二氧化钛系统的负极活性物质116为含碳材料例如石墨化中间相碳微球(MCMB)。过氧化锂/碳硫复合物系统的负极活性物质116可为含碳材料例如硬碳。本发明的锂离子提供者可为过氧化锂,但不限于过氧化锂,例如氧化锂亦可适用。或者,将过氧化锂与氧化锂混合使用。另外,正极框架活性物质也可以选择含碳材料,如此正、负极皆为含碳材料而形成锂离子电容。具有高的质量比容量的氟碳(CFx)材料亦适合作为本发明的正极框架活性物质。具有极高的理论电容量的Si合金或Sn合金也适合作为本发明的负极活性物质116。 FIG. 1 shows a unit cell structure of a lithium ion energy storage device according to an embodiment of the present invention. The lithium ion energy storage device of this embodiment includes a plurality of unit cell structures 100 , and each unit cell structure 100 includes a porous separator 104 sandwiched between the positive electrode 106 and the negative electrode 108 . The porous separator 104 is coated with an adhesive 105 to increase the connectivity between the components of the battery structure 100 . The positive electrode 106 includes a first collector sheet 110 and a positive active material 114 on the first collector sheet 110 , and the negative electrode 108 includes a second collector sheet 112 and a negative active material 116 on the second collector sheet 112 . The positive active material 114 includes a lithium ion provider and a positive frame active material, wherein the lithium ion provider can be lithium peroxide, and the positive frame active material is such as anatase titanium dioxide or carbon-sulfur complex. The ratio of sulfur to carbon in the carbon-sulfur compound is 5~7:3~5. The negative electrode active material 116 of the lithium peroxide/titanium dioxide system is a carbonaceous material such as graphitized mesocarbon microspheres (MCMB). The negative electrode active material 116 of the lithium peroxide/carbon-sulfur composite system can be a carbonaceous material such as hard carbon. The lithium ion provider of the present invention can be lithium peroxide, but not limited to lithium peroxide, for example lithium oxide is also applicable. Alternatively, lithium peroxide is used in combination with lithium oxide. In addition, carbon-containing materials can also be selected as the positive frame active material, so that both the positive and negative electrodes are made of carbon-containing materials to form a lithium-ion capacitor. Fluorocarbon (CF x ) materials with high mass specific capacity are also suitable as the positive electrode frame active material of the present invention. Si alloy or Sn alloy having extremely high theoretical capacitance is also suitable as the negative electrode active material 116 of the present invention.
适合过氧化锂/二氧化钛系统的电解质可为含有锂盐例如LiPF6、LiClO4或LiBF4及有机溶剂,例如选自由碳酸乙烯酯、碳酸二乙酯及碳酸二乙酯构成的组群。适合过氧化锂/碳硫复合物系统的电解质可为四乙二醇二甲醚(TEGDME)和1,3-二氧戊烷(DOL)的混合体积比为1:1的混合溶液中溶解有1M浓度的双三氟甲基磺酸亚酰胺锂。 A suitable electrolyte for the lithium peroxide/titanium dioxide system may contain a lithium salt such as LiPF 6 , LiClO 4 or LiBF 4 and an organic solvent, for example selected from the group consisting of ethylene carbonate, diethyl carbonate and diethyl carbonate. The electrolyte suitable for the lithium peroxide/carbon-sulfur complex system can be dissolved in a mixed solution of tetraethylene glycol dimethyl ether (TEGDME) and 1,3-dioxolane (DOL) with a volume ratio of 1:1. Lithium bistrifluoromethanesulfonimide at a concentration of 1M.
本实施例的单元电池结构100的充放电模式,当充电至适当电位时,包含过氧化锂的正极活性物质114被分解而生成锂离子与氧气,事先将锂离子嵌入作为负极108的含碳材料中。当放电时,位于负极108的锂离子经由电解液扩散至正极106并嵌入正极活性物质中,之后便可进行正常的充放电操作。 In the charging and discharging mode of the unit cell structure 100 of this embodiment, when charged to an appropriate potential, the positive electrode active material 114 containing lithium peroxide is decomposed to generate lithium ions and oxygen, and the lithium ions are inserted into the carbonaceous material of the negative electrode 108 in advance middle. When discharging, the lithium ions located in the negative electrode 108 diffuse to the positive electrode 106 through the electrolyte solution and are embedded in the positive electrode active material, and then normal charge and discharge operations can be performed.
首先进行过氧化锂的电性探讨,本发明欲利用电化学充电的方式将过氧化锂分解而产生锂离子,之后便可在不含锂离子正、负极材料的全电池中反复的嵌入嵌出。由于过氧化锂的导电度不高,可添加导电碳以增加过氧化锂的导电度。 First, the electrical properties of lithium peroxide are discussed. The present invention intends to use electrochemical charging to decompose lithium peroxide to generate lithium ions, which can then be repeatedly intercalated in full batteries that do not contain lithium ion positive and negative electrode materials. . Since the conductivity of lithium peroxide is not high, conductive carbon can be added to increase the conductivity of lithium peroxide.
本发明提供一种锂离子储能元件的制造方法,首先将过氧化锂和二氧化钛、导电碳(superP碳黑、KS6石墨或两者的组合)及聚偏氟乙烯(PVDF)以一定的重量比混合,并将其分散于N-甲基-2-吡咯烷酮(NMP)而得到浆料。然后将上述浆料倒在铝箔上,使用刮刀涂布机将浆料涂布成膜。将涂布好的的电极置入在80°c的烘箱中去除溶剂6小时,然后升温至120°c烘干4至6小时,由此制备过氧化锂/二氧化钛极片。 The invention provides a manufacturing method of a lithium ion energy storage element. First, lithium peroxide, titanium dioxide, conductive carbon (superP carbon black, KS6 graphite or a combination of both) and polyvinylidene fluoride (PVDF) are mixed in a certain weight ratio Mix and disperse it in N-methyl-2-pyrrolidone (NMP) to obtain a slurry. Then the above slurry was poured on the aluminum foil, and the slurry was coated into a film using a knife coater. Place the coated electrode in an oven at 80°C to remove the solvent for 6 hours, then raise the temperature to 120°C and dry it for 4 to 6 hours, thereby preparing a lithium peroxide/titanium dioxide pole piece.
使用上述制备的过氧化锂/二氧化钛极片、作为负极的石墨化中间相碳微球(MCMB)及多孔性隔离膜,将在碳酸亚乙酯(EC)和碳酸二乙酯(DEC)的混合体积比为1:1的混合溶液中溶解有1M浓度的LiPF6的电解质,注入上述过氧化锂极片和负极之间,由此制作全电池。本发明的正极活性物质中的锂离子提供者可为过氧化锂,但不限于过氧化锂,例如氧化锂亦可适用。或者,将过氧化锂与氧化锂混合使用。另外,正极框架活性物质也可以选择含碳材料,如此正、负极皆为含碳材料而形成锂离子电容。具有高的质量比容量的氟碳材料亦适合作为本发明的正极框架活性物质。具有极高的理论电容量的Si合金或Sn合金也适合作为本发明的负极活性物质116。 Using the lithium peroxide/titanium dioxide pole piece prepared above, the graphitized mesocarbon microspheres (MCMB) as the negative electrode and the porous separator, the mixture of ethylene carbonate (EC) and diethyl carbonate (DEC) An electrolyte in which 1M concentration of LiPF 6 is dissolved in a mixed solution with a volume ratio of 1:1 is injected between the above-mentioned lithium peroxide electrode sheet and the negative electrode, thereby producing a full battery. The lithium ion provider in the positive electrode active material of the present invention may be lithium peroxide, but is not limited to lithium peroxide, for example lithium oxide may also be applicable. Alternatively, lithium peroxide is used in combination with lithium oxide. In addition, carbon-containing materials can also be selected as the positive frame active material, so that both the positive and negative electrodes are made of carbon-containing materials to form a lithium-ion capacitor. Fluorocarbon materials with high mass specific capacity are also suitable as the positive electrode frame active material of the present invention. Si alloy or Sn alloy having extremely high theoretical capacitance is also suitable as the negative electrode active material 116 of the present invention.
本发明另外提供一种锂离子储能元件的制造方法,首先将过氧化锂和正极框架活性物质,例如碳硫复合物、导电碳(superP碳黑、KS6石墨或两者的组合)及粘着剂例如羧甲基纤维素(CMC)以一定的重量比混合,并将其分散于N-甲基-2-吡咯烷酮而得到浆料。然后将上述浆料倒在铝箔上,使用刮刀涂布机将浆料涂布成膜。将涂布好的的电极置入在80~90°c的烘箱中去除溶剂,然后升温至120~130°c烘干一段时间,由此制备过氧化锂/碳硫复合物极片。本发明的正极活性物质中的锂离子提供者可为过氧化锂,但不限于过氧化锂,例如氧化锂亦可适用。或者,将过氧化锂与氧化锂混合使用。另外,正极框架活性物质也可以选择含碳材料,如此正、负极皆为含碳材料而形成锂离子电容。具有高的质量比容量的氟碳材料亦适合作为本发明的正极框架活性物质。具有极高的理论电容量的Si合金或Sn合金也适合作为本发明的负极活性物质116。 The present invention additionally provides a manufacturing method of a lithium-ion energy storage element. Firstly, lithium peroxide and positive frame active materials, such as carbon-sulfur composites, conductive carbon (superP carbon black, KS6 graphite or a combination of the two) and an adhesive For example, carboxymethyl cellulose (CMC) is mixed in a certain weight ratio and dispersed in N-methyl-2-pyrrolidone to obtain a slurry. Then the above slurry was poured on the aluminum foil, and the slurry was coated into a film using a knife coater. Place the coated electrode in an oven at 80-90°C to remove the solvent, then heat up to 120-130°C and dry for a period of time, thereby preparing a lithium peroxide/carbon-sulfur composite pole piece. The lithium ion provider in the positive electrode active material of the present invention may be lithium peroxide, but is not limited to lithium peroxide, for example lithium oxide may also be applicable. Alternatively, lithium peroxide is used in combination with lithium oxide. In addition, carbon-containing materials can also be selected as the positive frame active material, so that both the positive and negative electrodes are made of carbon-containing materials to form a lithium-ion capacitor. Fluorocarbon materials with high mass specific capacity are also suitable as the positive electrode frame active material of the present invention. Si alloy or Sn alloy having extremely high theoretical capacitance is also suitable as the negative electrode active material 116 of the present invention.
使用上述制备的过氧化锂/碳硫复合物极片、作为负极的硬碳及多孔性隔离膜,将在四乙二醇二甲醚(TEGDME)和1,3-二氧戊烷(DOL)的混合体积比为1:1的混合溶液中溶解有1M浓度的双三氟甲基磺酸亚酰胺锂的电解质,注入上述过氧化锂极片和负极之间,由此制作全电池。 Use the above-mentioned lithium peroxide/carbon-sulfur composite pole sheet prepared above, as the hard carbon of the negative pole and the porous separator, will be in tetraethylene glycol dimethyl ether (TEGDME) and 1,3-dioxolane (DOL) An electrolyte in which lithium bistrifluoromethanesulfonate imide at a concentration of 1M is dissolved in a mixed solution with a mixing volume ratio of 1:1 is injected between the lithium peroxide pole piece and the negative electrode, thereby producing a full battery.
(性能测试) (Performance Testing)
图2为本发明过氧化锂的半电池充放电的电压对电容量的第1循环曲线图。图3为本发明过氧化锂的半电池充放电的电压对电容量的第2和3循环曲线图。操作条件如下:将过氧化锂、碳黑(superP)及聚偏氟乙烯(PVDF)分别以10:80:10的重量比混合所制备的正极,与将在碳酸亚乙酯(EC)和碳酸二乙酯(DEC)的混合体积比为1:1的混合溶液中溶解有1M浓度的LiPF6的电解质,注入多孔性隔离膜中组成半电池。充放电电流为100mA/g过氧化锂,充放电电压为2~4.6V。 Fig. 2 is the first cycle graph of the voltage versus the capacity of the lithium peroxide half-cell charge and discharge of the present invention. Fig. 3 is the 2nd and 3rd cycle graphs of the voltage versus the capacity of the lithium peroxide half-cell charge and discharge of the present invention. The operating conditions are as follows: the positive electrode prepared by mixing lithium peroxide, carbon black (superP) and polyvinylidene fluoride (PVDF) in a weight ratio of 10:80:10 is mixed with ethylene carbonate (EC) and carbonic acid Diethyl ester (DEC) with a mixing volume ratio of 1:1 is dissolved in a mixed solution with a concentration of 1M LiPF 6 electrolyte, which is injected into a porous separator to form a half-cell. The charge and discharge current is 100mA/g lithium peroxide, and the charge and discharge voltage is 2~4.6V.
图4是本发明过氧化锂于不同导电碳比例下的半电池充放电的电压对电容量的第1循环曲线图。操作条件如下:将过氧化锂、导电碳(superP碳黑:KS6石墨=1:1)及聚偏氟乙烯(PVDF)分别以X:Y:10的重量比混合所制备的正极,其中X=80、60、45、30、10,以及Y=10、30、45、60、80与将在碳酸亚乙酯(EC)和碳酸二乙酯(DEC)的混合体积比为1:1的混合溶液中溶解有1M浓度的LiPF6的电解质,注入多孔性隔离膜中组成半电池。充放电电流为10mA/g过氧化锂,充放电电压为2~4.8V。 Fig. 4 is the first cycle graph of the voltage versus capacity of half-cell charging and discharging of lithium peroxide of the present invention under different conductive carbon ratios. The operating conditions are as follows: the positive electrode prepared by mixing lithium peroxide, conductive carbon (superP carbon black: KS6 graphite = 1:1) and polyvinylidene fluoride (PVDF) in a weight ratio of X:Y:10, where X= 80, 60, 45, 30, 10, and Y=10, 30, 45, 60, 80 and the mixing volume ratio of ethylene carbonate (EC) and diethyl carbonate (DEC) is 1:1 An electrolyte with 1M concentration of LiPF 6 dissolved in the solution is injected into a porous separator to form a half-cell. The charging and discharging current is 10mA/g lithium peroxide, and the charging and discharging voltage is 2~4.8V.
图5是过氧化锂和导电碳不同比例下的循环电位扫描。操作条件如下:扫描速率为0.4mV/s,过氧化锂:导电碳=X:Y,其中X:Y为10:80及30:60。碳酸亚乙酯(EC)和碳酸二乙酯(DEC)的混合体积比为1:1的混合溶液中溶解有1M浓度的LiPF6的电解质的循环电位扫描的电流在不同电压下皆为0mA。 Figure 5 is a cycle potential scan at different ratios of lithium peroxide and conductive carbon. The operating conditions are as follows: the scan rate is 0.4mV/s, lithium peroxide: conductive carbon = X: Y, where X: Y is 10:80 and 30:60. Ethylene carbonate (EC) and diethyl carbonate (DEC) with a mixing volume ratio of 1:1 in the mixed solution with 1M concentration of LiPF 6 dissolved in the cyclic potential sweep current of the electrolyte is 0mA at different voltages.
图6显示不同电流密度对于过氧化锂的电压对电容量的影响。操作条件如下:将过氧化锂、导电碳(superP碳黑:KS6石墨=1:1)及聚偏氟乙烯(PVDF)分别以30:60:10的重量比混合所制备的正极,与将在碳酸亚乙酯(EC)和碳酸二乙酯(DEC)的混合体积比为1:1的混合溶液中溶解有1M浓度的LiPF6的电解质,注入多孔性隔离膜中组成半电池。充放电电流分别为10mA/g过氧化锂、30mA/g过氧化锂及50mA/g过氧化锂,充放电电压为2~4.8V。 Figure 6 shows the effect of different current densities on the voltage of lithium peroxide on the capacity. The operating conditions are as follows: the positive electrode prepared by mixing lithium peroxide, conductive carbon (superP carbon black: KS6 graphite = 1:1) and polyvinylidene fluoride (PVDF) in a weight ratio of 30:60:10, and the A mixed solution of ethylene carbonate (EC) and diethyl carbonate (DEC) with a mixing volume ratio of 1:1 is dissolved with an electrolyte of 1M concentration of LiPF 6 and injected into a porous separator to form a half-cell. The charging and discharging currents are 10mA/g lithium peroxide, 30mA/g lithium peroxide and 50mA/g lithium peroxide respectively, and the charging and discharging voltage is 2~4.8V.
以上说明过氧化锂、导电碳及粘着剂之间的搭配,以及电流密度对过氧化锂充放电的影响。然而,正极端的过氧化锂属一次性功能性材料,即只能进行一次充电分解。因此,在放电过程中,需另有活性物质接收从负极扩散至正极的锂离子,例如锐钛矿相二氧化钛或碳硫复合物。 The above describes the combination of lithium peroxide, conductive carbon and adhesive, and the influence of current density on the charge and discharge of lithium peroxide. However, the lithium peroxide at the positive end is a disposable functional material, that is, it can only be decomposed by one charge. Therefore, during the discharge process, another active material is required to receive lithium ions diffused from the negative electrode to the positive electrode, such as anatase phase titanium dioxide or carbon-sulfur complex.
本发明将起始过氧化锂充电分解出锂离子扩散至负极以及放电锂离子从负极扩散至正极分别称为预置锂充电阶段及预置锂放电阶段,而后续锂电池在二氧化钛正极与负极进行嵌入嵌出则为真正工作系统。 In the present invention, the initial lithium peroxide charging and decomposing lithium ions diffused to the negative electrode and the discharged lithium ions diffused from the negative electrode to the positive electrode are respectively called the preset lithium charging stage and the preset lithium discharging stage, and the subsequent lithium battery is carried out at the titanium dioxide positive electrode and the negative electrode. Embedding and embedding is a real working system.
请参考图7及图8,图7为过氧化锂/二氧化钛对Li/Li+的半电池预置锂充放电曲线,以及图8为预置锂阶段后的二氧化钛的充放电曲线。在预置锂充电阶段,先对过氧化锂以50mA/gLi2O2的电流密度充电至4.8V对Li/Li+,而在预置锂的放电阶段及后续的充放电则对二氧化钛以0.1C(1C=335mAh/g)于1~3V对Li/Li+的范围进行充放电,其半电池充放电曲线如图7及图8所示。图7中分为过氧化锂充电曲线(预置锂充电阶段)及二氧化钛放电曲线(预置锂放电阶段),预置锂充电阶段的电容量为365mA/gLi2O2,而预置锂放电阶段有1.8V和2.7V两个放电平台,2.7V平台的电容量约为100mAh/gTiO2,其可能为氧化还原反应或是过氧化锂的再生成,在本系统中视为副反应,即多出的电容量并非属二氧化钛所有。此外,在将由副反应贡献的电容量扣除后得到的电容量约为280mAh/gTiO2。 Please refer to FIG. 7 and FIG. 8 . FIG. 7 is the charge-discharge curve of lithium peroxide/titanium dioxide on Li/Li + half-cell preset lithium, and FIG. 8 is the charge-discharge curve of titanium dioxide after the lithium-preset stage. In the charging stage of preset lithium, charge lithium peroxide to 4.8V vs. Li/Li + at a current density of 50mA/gLi 2 O 2 , and charge titanium dioxide at 0.1 in the discharging stage of preset lithium and subsequent charging and discharging C (1C=335mAh/g) charges and discharges Li/Li + at 1~3V, and its half-cell charge and discharge curves are shown in Figure 7 and Figure 8. Figure 7 is divided into lithium peroxide charging curve (preset lithium charging stage) and titanium dioxide discharge curve (preset lithium discharge stage), the capacity of the preset lithium charging stage is 365mA/gLi 2 O 2 There are two discharge platforms, 1.8V and 2.7V, and the capacity of the 2.7V platform is about 100mAh/gTiO 2 , which may be a redox reaction or the regeneration of lithium peroxide. The capacitance shown is not owned by titanium dioxide. In addition, the capacitance obtained after deducting the capacitance contributed by the side reaction was about 280 mAh/g TiO 2 .
接着,请参考图9及图10。图9为过氧化锂/二氧化钛对石墨化中间相碳微球(MCMB)的全电池预置锂充放电曲线,以及图10为预置锂阶段后的二氧化钛的充放电曲线。于此实验中使用负极为MCMB,其涂布粉末重量比例为活性物质:superP碳黑:KS石墨:粘着剂为70:7.5:7.5:15,而正极材料的过氧化锂、导电碳、粘着剂及二氧化钛则相对MCMB粉末重以A/C比率=1的方式涂布。相对于MCMB的电容量,计算出过氧化锂、superP碳黑、KS石墨的重量各为0.4219g(22%),而PVDF及二氧化钛的重量分别为0.1406g(7%)及0.4858g(27%)。在预置锂充电阶段,先对过氧化锂以50mA/gLi2O2的电流密度充电至4.8V对MCMB,而在预置锂的放电阶段及后续的充放电则对二氧化钛以0.1C(1C=335mAh/g)于0~3V对MCMB的范围进行充放电,其全电池充放电曲线如图9及图10所示。 Next, please refer to FIG. 9 and FIG. 10 . Figure 9 is the full battery preset lithium charge and discharge curve of lithium peroxide/titanium dioxide on graphitized mesocarbon microspheres (MCMB), and Figure 10 is the charge and discharge curve of titanium dioxide after the lithium preset stage. In this experiment, the negative pole MCMB is used, and the weight ratio of the coated powder is active material: superP carbon black: KS graphite: binder is 70:7.5:7.5:15, while the positive electrode material lithium peroxide, conductive carbon, binder And titanium dioxide is coated with the weight of A/C ratio = 1 relative to the MCMB powder. Relative to the capacitance of MCMB, the weights of lithium peroxide, superP carbon black, and KS graphite are calculated to be 0.4219g (22%), while the weights of PVDF and titanium dioxide are 0.1406g (7%) and 0.4858g (27%) respectively. ). In the charging stage of preset lithium, first charge lithium peroxide to 4.8V for MCMB with a current density of 50mA/gLi 2 O 2 , and charge titanium dioxide at 0.1C (1C =335mAh/g) charge and discharge MCMB in the range of 0~3V, and the charge and discharge curves of the full battery are shown in Figure 9 and Figure 10.
由上述,可知预置锂离子于正极的方法确实可行,但是过程中会产生氧气,而影响电化学的表现。因此,氧气的去除对锂离子电池的性能表现是重要的。在大型锂电池如铝箔软包电池的制作过程中,会进行活化动作,即注入电解质后进行首圈充放电以形成负极的固态电解质介面膜,此时电解质会部分裂解,利用抽真空方式将电解质抽出后再注入新的电解质,即可进行正常充放电。图11系显示具有去除氧气的过氧化锂/二氧化钛对石墨化中间相碳微球(MCMB)的全电池预置锂充放电曲线,以及图12为具有去除氧气的预置锂阶段后的二氧化钛的充放电曲线。从图11尚无法看出去除氧气后的效果,但从图12后续二氧化钛充放电过程中电容量并无剧烈衰退,可证实后续的充放电确实受到预置锂放电阶段的副反应影响,而副反应的源头则为预置锂充电过程过氧化锂所分解出来的氧气。 From the above, it can be seen that the method of presetting lithium ions on the positive electrode is indeed feasible, but oxygen will be generated during the process, which will affect the electrochemical performance. Therefore, the removal of oxygen is important to the performance of Li-ion batteries. In the production process of large-scale lithium batteries such as aluminum foil pouch batteries, the activation action will be carried out, that is, the first round of charge and discharge will be performed after injecting the electrolyte to form a solid electrolyte interface film of the negative electrode. At this time, the electrolyte will be partially cracked, and the electrolyte will be vacuumed After pulling out and injecting new electrolyte, normal charge and discharge can be carried out. Figure 11 shows the charge-discharge curves of lithium peroxide/titanium dioxide for graphitized mesocarbon microspheres (MCMB) with full-cell pre-set Li with oxygen removal, and Figure 12 for TiO after the pre-lithium stage with oxygen removal. charge and discharge curve. The effect of removing oxygen cannot be seen from Figure 11, but from Figure 12 there is no drastic decline in the capacity during the subsequent charging and discharging of titanium dioxide, which proves that the subsequent charging and discharging are indeed affected by the side reactions of the preset lithium discharge stage, and the side effects The source of the reaction is the oxygen decomposed by lithium peroxide during the preset lithium charging process.
另一实施例中,正极活性物质中的正极框架活性物质可使用碳硫复合物。将过氧化锂与碳硫复合物混合,以取代锂金属,并利用硬碳作为负极组成全电池。由于锂硫电池的电解质为醚类,本实施例使用过氧化锂:导电碳:粘着剂=30:60:10的重量比,于1M双三氟甲基磺酸亚酰胺锂(LiTFSI)/四乙二醇二甲醚(TEGDME):1,3-二氧戊烷(DOL)=1:1(v:v)以100mA/gLi2O2的电流密度相对于锂金属于2~4.3V进行半电池测试,如图13所示。选用充电截止电压为4.3V,选用100mA/gLi2O2进行充电大约9小时。可发现锂硫电池电解质系统中的过氧化锂分解过电位约为4.1V,且所得的电容量约为980mAh/gLi2O2。 In another embodiment, the positive frame active material in the positive active material may use a carbon-sulfur compound. Lithium peroxide is mixed with carbon-sulfur complex to replace lithium metal, and hard carbon is used as the negative electrode to form a full battery. Since the electrolyte of the lithium-sulfur battery is ether, this embodiment uses lithium peroxide: conductive carbon: adhesive = 30:60:10 weight ratio, in 1M lithium bistrifluoromethanesulfonate imide (LiTFSI) / four Ethylene glycol dimethyl ether (TEGDME): 1,3-dioxolane (DOL) = 1: 1 (v: v) at a current density of 100mA/gLi 2 O 2 against lithium metal at 2~4.3V Half-cell test, as shown in Figure 13. The charging cut-off voltage is selected as 4.3V, and 100mA/gLi 2 O 2 is selected for charging for about 9 hours. It can be found that the lithium peroxide decomposition overpotential in the lithium-sulfur battery electrolyte system is about 4.1V, and the obtained electric capacity is about 980mAh/gLi 2 O 2 .
图14显示碳硫复合物电极组成半电池的充放电曲线。将碳硫复合物电极组成半电池,其中硫碳比例为5~7:3~5。之后以0.1C(1C=1672mAh/gs)的充放电速率于1.5~3V对Li/Li+进行充放电,充放电曲线如图14所示。 Figure 14 shows the charge-discharge curves of the half-cell composed of carbon-sulfur composite electrodes. A carbon-sulfur composite electrode is used to form a half-cell, in which the ratio of sulfur to carbon is 5~7:3~5. Then charge and discharge Li/Li + at 1.5~3V at a charge and discharge rate of 0.1C (1C=1672mAh/gs), and the charge and discharge curve is shown in Figure 14.
图15是过氧化锂/碳硫复合物对Li/Li+的半电池预置锂充放电曲线。在确认过氧化锂及碳硫复合物各别的电化学表现后,本实施例将上述两种材料混合作成电极,制备电极时以N-甲基-2-吡咯烷酮作为分散剂,并以100mA/gLi2O2的电流密度在预置锂充电阶段对过氧化锂进行充电至4.3V对Li/Li+,再以0.1C(1C=1672mAh/gs)对碳硫复合物进行预置锂放电及后续的充放电。预置锂充电阶段与放电阶段的充放电曲线,如图15所示。 Fig. 15 is the lithium peroxide/carbon sulfur compound's half-cell preset lithium charge and discharge curves for Li/Li + . After confirming the respective electrochemical performances of lithium peroxide and carbon-sulfur complexes, in this embodiment, the above two materials are mixed to make an electrode. When preparing the electrode, N-methyl-2-pyrrolidone is used as a dispersant, and 100mA/ The current density of gLi 2 O 2 charges lithium peroxide to 4.3V for Li/Li + in the preset lithium charging stage, and then performs preset lithium discharge and Subsequent charge and discharge. The charging and discharging curves of the preset lithium charging stage and discharging stage are shown in Figure 15.
本发明利用电化学充电的方式将过氧化锂及/或氧化锂分解,产生锂离子,之后便可在正极框架活性物质、负极活性物质的全电池中反复的嵌入与嵌出,可展示高的电容量。正极框架活性物质可为锐钛矿相二氧化钛、碳硫复合物、含碳材料或氟碳材料,但不限于此,只要是稳定性高及具有良好电容量的材料皆可适用。甚至使用锂金属氧化物作为正极框架活性物质,与过氧化锂及/或氧化锂结合作为正极活性物质,也可展示比单纯使用锂金属氧化物作为正极活性物质高的电容量。 The present invention uses electrochemical charging to decompose lithium peroxide and/or lithium oxide to generate lithium ions, which can then be repeatedly embedded and embedded in the full battery of positive frame active materials and negative electrode active materials, and can exhibit high capacitance. The positive frame active material can be anatase phase titanium dioxide, carbon-sulfur composite, carbonaceous material or fluorocarbon material, but not limited thereto, as long as it is a material with high stability and good capacitance. Even using lithium metal oxide as the positive electrode frame active material, combined with lithium peroxide and/or lithium oxide as the positive electrode active material, can also exhibit a higher capacity than using lithium metal oxide alone as the positive electrode active material.
以上所述实施例仅是为充分说明本发明而所举的较佳的实施例,本发明的保护范围不限于此。本技术领域的技术人员在本发明基础上所作的等同替代或变换,均在本发明的保护范围之内。本发明的保护范围以权利要求书为准。 The above-mentioned embodiments are only preferred embodiments for fully illustrating the present invention, and the protection scope of the present invention is not limited thereto. Equivalent substitutions or transformations made by those skilled in the art on the basis of the present invention are all within the protection scope of the present invention. The protection scope of the present invention shall be determined by the claims.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108550796A (en) * | 2018-04-12 | 2018-09-18 | 上海空间电源研究所 | Closed lithium-oxygen battery lithia-fluorocarbons anode pole piece and preparation method thereof |
CN110100335A (en) * | 2016-12-21 | 2019-08-06 | 罗伯特·博世有限公司 | Lithium ion battery and preparation method thereof |
CN112615043A (en) * | 2020-08-26 | 2021-04-06 | 清陶(昆山)能源发展有限公司 | All-solid-state lithium ion battery |
CN113574697A (en) * | 2019-01-15 | 2021-10-29 | 麦斯韦尔技术股份有限公司 | Compositions and methods for prelithiated energy storage devices |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050106460A1 (en) * | 2002-02-25 | 2005-05-19 | Masashi Otsuki | Positive electrode for nonaqueous electrolyte battery, process for producing the same and nonaqueous electrolyte battery |
CN102227833A (en) * | 2009-04-27 | 2011-10-26 | 松下电器产业株式会社 | Positive electrode plate for nonaqueous electrolyte secondary battery, method for producing same, and nonaqueous electrolyte secondary battery |
US20120328955A1 (en) * | 2011-06-27 | 2012-12-27 | Hyundai Motor Company | Lithium secondary battery having high capacity |
US20140212755A1 (en) * | 2013-01-29 | 2014-07-31 | Uchicago Argonne, Llc | Electroactive materials for rechargeable batteries |
US20140217992A1 (en) * | 2013-02-05 | 2014-08-07 | Hrl Laboratories, Llc | Separators for lithium-sulfur batteries |
-
2014
- 2014-11-13 CN CN201410639412.XA patent/CN105655646A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050106460A1 (en) * | 2002-02-25 | 2005-05-19 | Masashi Otsuki | Positive electrode for nonaqueous electrolyte battery, process for producing the same and nonaqueous electrolyte battery |
CN102227833A (en) * | 2009-04-27 | 2011-10-26 | 松下电器产业株式会社 | Positive electrode plate for nonaqueous electrolyte secondary battery, method for producing same, and nonaqueous electrolyte secondary battery |
US20120328955A1 (en) * | 2011-06-27 | 2012-12-27 | Hyundai Motor Company | Lithium secondary battery having high capacity |
US20140212755A1 (en) * | 2013-01-29 | 2014-07-31 | Uchicago Argonne, Llc | Electroactive materials for rechargeable batteries |
US20140217992A1 (en) * | 2013-02-05 | 2014-08-07 | Hrl Laboratories, Llc | Separators for lithium-sulfur batteries |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110100335A (en) * | 2016-12-21 | 2019-08-06 | 罗伯特·博世有限公司 | Lithium ion battery and preparation method thereof |
CN108550796A (en) * | 2018-04-12 | 2018-09-18 | 上海空间电源研究所 | Closed lithium-oxygen battery lithia-fluorocarbons anode pole piece and preparation method thereof |
CN113574697A (en) * | 2019-01-15 | 2021-10-29 | 麦斯韦尔技术股份有限公司 | Compositions and methods for prelithiated energy storage devices |
US11949089B2 (en) | 2019-01-15 | 2024-04-02 | Tesla, Inc. | Compositions and methods for prelithiating energy storage devices |
CN113574697B (en) * | 2019-01-15 | 2025-01-10 | 麦斯韦尔技术股份有限公司 | Compositions and methods for pre-lithiation energy storage devices |
CN112615043A (en) * | 2020-08-26 | 2021-04-06 | 清陶(昆山)能源发展有限公司 | All-solid-state lithium ion battery |
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