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CN116014363A - A kind of preparation method of composite current collecting and separating layer - Google Patents

A kind of preparation method of composite current collecting and separating layer Download PDF

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CN116014363A
CN116014363A CN202111232547.0A CN202111232547A CN116014363A CN 116014363 A CN116014363 A CN 116014363A CN 202111232547 A CN202111232547 A CN 202111232547A CN 116014363 A CN116014363 A CN 116014363A
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current collector
porous
electrode current
porous electrode
preparation
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何颖源
侯凯
杨景刚
张彬
陈永翀
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Institute of Electrical Engineering of CAS
Electric Power Research Institute of State Grid Jiangsu Electric Power Co Ltd
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Institute of Electrical Engineering of CAS
Electric Power Research Institute of State Grid Jiangsu Electric Power Co Ltd
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    • Y02E60/10Energy storage using batteries

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Abstract

The invention provides a preparation method of a composite current collecting isolation layer. In the preparation method, a porous electrode current collector is placed on a plurality of stainless steel wires, and an arch part is formed on the porous electrode current collector by heating and pressurizing treatment, wherein the section of the arch part is in an arch shape with one concave surface and one convex surface. The porous electrode current collector and the diaphragm are combined into a whole, and a flow channel for electrolyte is formed between the concave part of the arch part of the porous electrode current collector and the diaphragm, so that the electrolyte can enter the electrode plate rapidly through the flow channel, and the electrolyte in the flow channel is injected into the electrode material layer through the through holes of the porous electrode current collector, so that the electrode material layer in the electrode plate can be infiltrated rapidly. In the composite current collecting isolation layer, burrs at the edges of the porous electrode current collector are flattened, and the edges of the separator are subjected to edge wrapping composite treatment on the porous electrode current collector, so that short circuit of the battery caused by contact of the burrs at the edges of the porous electrode current collector can be effectively prevented.

Description

一种复合集流隔离层的制备方法A kind of preparation method of composite current collecting and separating layer

技术领域technical field

本发明涉及锂浆料电池领域,具体地涉及一种复合集流隔离层的制备方法。The invention relates to the field of lithium slurry batteries, in particular to a preparation method of a composite current collecting and separating layer.

背景技术Background technique

锂浆料电池是一种新型的锂电池。锂浆料电池具有三维多孔的电芯结构,且电极材料层中含有一定比例非粘接固定的导电颗粒,可以在电解液中形成动态的导电网络,避免传统锂离子电池电极材料脱落或松动造成的电池容量下降和循环寿命衰减等问题。大容量锂浆料电池具有注排液的功能,其电极厚度是传统锂离子电池的5~10倍,因此如在注排液的时候提供更多的通道供电解液进入会大大提高注排液的效率,有利于电极内部液体的浸润;而且由于采用厚电极结构,在电芯内部提供更多的散热排气通道可以防止气泡等残留在电极片表面上影响电池正常的充放电反应。Lithium slurry battery is a new type of lithium battery. Lithium slurry battery has a three-dimensional porous cell structure, and the electrode material layer contains a certain proportion of non-adhesive and fixed conductive particles, which can form a dynamic conductive network in the electrolyte to avoid the traditional lithium-ion battery electrode material from falling off or loosening. problems such as battery capacity decline and cycle life attenuation. Large-capacity lithium slurry battery has the function of liquid injection and discharge, and its electrode thickness is 5 to 10 times that of traditional lithium-ion batteries. Therefore, if more channels are provided for electrolyte to enter during liquid injection and discharge, it will greatly improve the efficiency of liquid injection and discharge. The efficiency is conducive to the infiltration of the liquid inside the electrode; and because of the thick electrode structure, more cooling and exhaust channels are provided inside the cell to prevent bubbles and other residues on the surface of the electrode sheet from affecting the normal charge and discharge reaction of the battery.

发明内容Contents of the invention

针对以上存在的问题,本发明提供一种复合集流隔离层的制备方法。在该制备方法中,将多孔电极集流体置于多条不锈钢丝上面,利用加热加压处理在多孔电极集流体上形成拱形部,拱形部的截面为一面凹进并且一面凸起的拱形。将多孔电极集流体与隔膜复合为一体,在多孔电极集流体的拱形部的凹进部分与隔膜之间形成用于电解液的流动通道,有利于电解液经由流动通道快速进入电极片内部,流动通道内的电解液经由多孔电极集流体的通孔注入电极材料层,从而可以快速浸润电极片内的电极材料层。在复合集流隔离层中,多孔电极集流体边缘的毛刺被压平并且隔膜的边缘对多孔电极集流体进行包边复合处理,可以有效防止多孔电极集流体边缘的毛刺接触导致的电池短路。In view of the above existing problems, the present invention provides a method for preparing a composite current collecting and separating layer. In this preparation method, the porous electrode current collector is placed on a plurality of stainless steel wires, and an arched part is formed on the porous electrode current collector by means of heat and pressure treatment. The cross section of the arched part is an arch with one side concave and one side convex shape. Combining the porous electrode current collector with the diaphragm, a flow channel for the electrolyte is formed between the concave part of the arched part of the porous electrode collector and the diaphragm, which is conducive to the rapid entry of the electrolyte into the electrode sheet through the flow channel. The electrolyte solution in the flow channel is injected into the electrode material layer through the through holes of the porous electrode collector, so that the electrode material layer in the electrode sheet can be quickly wetted. In the composite current collector separation layer, the burrs on the edge of the porous electrode collector are flattened and the edge of the separator wraps the porous electrode collector, which can effectively prevent the short circuit of the battery caused by the contact of the burr on the edge of the porous electrode collector.

本发明提供的技术方案如下:The technical scheme provided by the invention is as follows:

根据本发明提供一种复合集流隔离层的制备方法,该制备方法包括如下步骤:According to the present invention there is provided a method for preparing a composite current collecting and isolating layer, the method comprising the following steps:

(a)在多孔电极集流体的下方铺设多条不锈钢丝,至少部分不锈钢丝的端部延伸超出多孔电极集流体的边缘;(a) laying a plurality of stainless steel wires under the porous electrode current collector, at least some of the ends of the stainless steel wires extend beyond the edge of the porous electrode current collector;

(b)采用压力机对多孔电极集流体进行加热加压处理,多孔电极集流体在与不锈钢丝接触的部位弯曲变形,从而在多孔电极集流体上形成一面凹进并且一面凸起的拱形部;(b) Use a press to heat and press the porous electrode current collector, and the porous electrode current collector is bent and deformed at the part in contact with the stainless steel wire, thereby forming an arched part with one side concave and one side convex on the porous electrode current collector ;

(c)在多孔电极集流体的拱形部的凹进的一面上,多孔电极集流体的平面部分与隔膜复合,多孔电极集流体的拱形部的凹进部分与隔膜之间形成流动通道,同时隔膜的边缘对多孔电极集流体进行包边复合处理。(c) On the concave side of the arched part of the porous electrode current collector, the planar part of the porous electrode current collector is combined with the diaphragm, and a flow channel is formed between the concave part of the arched part of the porous electrode current collector and the diaphragm, At the same time, the edge of the diaphragm is subjected to edge-wrapping composite treatment on the porous electrode current collector.

多孔电极集流体可以为多孔正极集流体,多孔正极集流体可以为具有通孔结构的厚度为1μm~2000μm的电子导电层,多孔正极集流体的孔径可以为0.01μm~2000μm,通孔孔隙率可以为10%~90%。多孔正极集流体可以为导电金属层,导电金属层可以为金属网或金属丝编织网;或者,导电金属层可以为具有通孔结构的泡沫金属网;或者,导电金属层可以为多孔金属板或多孔金属箔。导电金属层的材料优选为铝。The porous electrode current collector can be a porous positive current collector, the porous positive current collector can be an electronically conductive layer with a through-hole structure with a thickness of 1 μm to 2000 μm, the pore diameter of the porous positive current collector can be 0.01 μm to 2000 μm, and the porosity of the through holes can be 10% to 90%. The porous positive current collector can be a conductive metal layer, and the conductive metal layer can be a metal mesh or a wire woven mesh; or, the conductive metal layer can be a foamed metal mesh with a through-hole structure; or, the conductive metal layer can be a porous metal plate or porous metal foil. The material of the conductive metal layer is preferably aluminum.

多孔电极集流体可以为多孔负极集流体,多孔负极集流体可以为具有通孔结构的厚度为1μm~2000μm的电子导电层,多孔负极集流体的孔径可以为0.01μm~2000μm,通孔孔隙率可以为10%~90%。多孔负极集流体可以为导电金属层,导电金属层可以为金属网或金属丝编织网;或者,导电金属层可以为具有通孔结构的泡沫金属网;或者,导电金属层可以为多孔金属板或多孔金属箔。导电金属层的材料优选为铜。The porous electrode current collector can be a porous negative electrode current collector, and the porous negative electrode current collector can be an electronically conductive layer with a through-hole structure with a thickness of 1 μm to 2000 μm. The pore diameter of the porous negative electrode current collector can be 0.01 μm to 2000 μm. 10% to 90%. The porous negative electrode current collector can be a conductive metal layer, and the conductive metal layer can be a metal mesh or a wire braided mesh; or, the conductive metal layer can be a foamed metal mesh with a through-hole structure; or, the conductive metal layer can be a porous metal plate or porous metal foil. The material of the conductive metal layer is preferably copper.

隔膜的材料可以为电子不导电的多孔聚合物材料;或者,隔膜的材料可以为电子不导电的无机非金属材料与有机聚合物复合的多孔材料;或者,隔膜的材料可以为电子不导电的聚合物基体、液体有机增塑剂和锂盐三部分复合构成的凝胶聚合物电解质复合材料;或者,隔膜的材料可以为在电子不导电的多孔聚合物材料的孔隙内或在无机非金属材料与有机聚合物复合的多孔材料的孔隙内浸渍有离子导电的电解液或聚合物胶体材料,等等。The material of the diaphragm can be an electronically non-conductive porous polymer material; or, the material of the diaphragm can be a porous material composed of an electronically non-conductive inorganic non-metallic material and an organic polymer; or, the material of the diaphragm can be an electronically non-conductive polymer A gel polymer electrolyte composite material composed of a three-part composite of a matrix, a liquid organic plasticizer, and a lithium salt; or, the material of the separator can be in the pores of an electronically non-conductive porous polymer material or in an inorganic non-metallic material and The pores of the organic polymer composite porous material are impregnated with an ion-conducting electrolyte or a polymer colloid material, and the like.

不锈钢丝可以直接置于多孔电极集流体的下方。或者,不锈钢丝可先铺设在用于固定不锈钢丝的模具中,然后再将多孔电极集流体置于不锈钢丝的上方。用于固定不锈钢丝的模具例如可以为刻有沟槽的块状模具,不锈钢丝可稳定地置于沟槽中。多条不锈钢丝的布置方式可以为平行方式、交叉方式、辐射方式等。优选地,多条不锈钢丝交叉铺设,从而在多孔电极集流体上形成相互交叉连通的通道,这样可以更加有利于电解液快速流向电极材料层的整个平面。另外,还可以设置不同直径的不锈钢丝,例如,设置具有较粗直径的总流道以及具有较细直径的分支流道,或者,沿着极片的长度方向设置具有较粗直径的大流量的流道。此外,不锈钢丝的形状可以为波浪形、Z字型、螺旋形等。可以根据需要灵活设置不锈钢丝的布置方式,根据极片尺寸增减不锈钢丝的数量,从而方便灵活地在电芯内形成可供电解液流通的流动通道。多条不锈钢丝中的至少部分不锈钢丝的端部从多孔电极集流体的边缘伸出,从而在将多个电极片堆叠成电芯之后,在多孔电极集流体的边缘形成用于电解液进入电芯内部的拱形开口。Stainless steel wire can be placed directly under the porous electrode current collector. Alternatively, the stainless steel wire can be first laid in a mold for fixing the stainless steel wire, and then the porous electrode current collector is placed on the stainless steel wire. The mold used to fix the stainless steel wire can be, for example, a block mold with grooves, and the stainless steel wire can be stably placed in the groove. The arrangement of multiple stainless steel wires can be parallel, cross, radial, etc. Preferably, a plurality of stainless steel wires are intersected to form cross-connected channels on the porous electrode current collector, which is more conducive to the rapid flow of the electrolyte to the entire plane of the electrode material layer. In addition, stainless steel wires of different diameters can also be provided, for example, a main channel with a larger diameter and a branch channel with a smaller diameter are provided, or a large flow channel with a larger diameter is provided along the length direction of the pole piece. runner. In addition, the shape of the stainless steel wire can be wavy, Z-shaped, spiral, etc. The layout of the stainless steel wires can be flexibly set according to the needs, and the number of stainless steel wires can be increased or decreased according to the size of the pole piece, so that a flow channel for the flow of the electrolyte can be formed conveniently and flexibly in the battery cell. The ends of at least some of the stainless steel wires protrude from the edge of the porous electrode collector, so that after the plurality of electrode sheets are stacked into a battery core, a hole for the electrolyte to enter the battery is formed at the edge of the porous electrode collector. Arched opening inside the core.

由于不锈钢材料的硬度高于铝或铜的硬度,因此当利用压力机将不锈钢丝与多孔铝网(多孔正极集流体)或与多孔铜网(多孔负极集流体)进行冲压时,会在多孔铝网和多孔铜网上形成诸如半圆形的拱形部分。不锈钢丝的直径可以为0.5~5mm,通过控制不锈钢丝的直径可以控制拱形部的尺寸。加热温度可以为50~200℃,加压压力可以为2~20MPa。通过控制加热温度,可以有利于多孔电极集流体的变形,并且可以在加压的同时实现加热复合隔膜的过程。Since the hardness of the stainless steel material is higher than that of aluminum or copper, when the stainless steel wire is stamped with a porous aluminum mesh (porous positive electrode current collector) or with a porous copper mesh (porous negative electrode current collector) by a press, the porous aluminum The mesh and perforated copper mesh form an arched portion such as a semicircle. The diameter of the stainless steel wire can be 0.5-5 mm, and the size of the arch can be controlled by controlling the diameter of the stainless steel wire. The heating temperature may be 50-200° C., and the pressing pressure may be 2-20 MPa. By controlling the heating temperature, the deformation of the porous electrode current collector can be facilitated, and the process of heating the composite separator can be realized while pressurizing.

多孔电极集流体的平面部分与隔膜复合的方式包括粘接或平面热压复合等,在平面热压复合的情况下,多孔集流体的通道挤压成型与隔膜热压复合可以同时完成,也就是说,步骤(b)与步骤(c)中除包边以外的部分可以同时一步完成。具体地讲,在多孔电极集流体的拱形部凹进的一面上,多孔电极集流体的未形成拱形部的部分与隔膜连接到一起,而多孔电极集流体的形成拱形部的部分不与隔膜连接到一起,在多孔电极集流体的拱形部的凹进部分与隔膜之间形成中空的流动通道,流动通道的截面形状例如可以为半圆形。通过将隔膜与多孔集流体拱形部的边缘平面部分复合固定,可以更好地保持多孔集流体的拱形部形状。The method of compounding the planar part of the porous electrode current collector and the diaphragm includes bonding or planar thermocompression compounding. Said, steps (b) and steps (c) can be completed in one step at the same time except for the hemming. Specifically, on the concave side of the arched portion of the porous electrode current collector, the portion of the porous electrode current collector that does not form the arched portion is connected to the separator, while the portion of the porous electrode current collector that forms the arched portion is not Connected with the diaphragm, a hollow flow channel is formed between the concave portion of the arched portion of the porous electrode collector and the diaphragm, and the cross-sectional shape of the flow channel may be, for example, a semicircle. By compounding and fixing the diaphragm and the edge plane part of the arched portion of the porous current collector, the shape of the arched portion of the porous current collector can be better maintained.

在多孔电极集流体的剪裁成形过程中,其边缘经常会出现垂直集流体平面的毛刺。当毛刺与隔膜直接接触时,容易刺破隔膜后与另一边的电极材料或者集流体接触,进而引发电池内部短路。在本发明中,当利用压力机在多孔电极集流体上压制流动通道时,同时可以将垂直于集流体平面的毛刺压平,另外,隔膜的尺寸稍大于多孔电极集流体的尺寸,使得隔膜的边缘延伸超出多孔电极集流体的边缘,将隔膜的边缘固定包覆于多孔电极集流体的边缘。这种压平并固定包覆(即,包边复合处理)的方式降低了毛刺刺破隔膜的风险,特别是采用胶粘方式固定包覆时,更是大大提高了电池的安全性。During the cutting and forming process of porous electrode current collectors, burrs perpendicular to the current collector plane often appear on the edges. When the burr is in direct contact with the separator, it is easy to pierce the separator and then contact the electrode material or current collector on the other side, thereby causing an internal short circuit of the battery. In the present invention, when the press is used to press the flow channel on the porous electrode collector, the burrs perpendicular to the plane of the collector can be flattened at the same time. In addition, the size of the diaphragm is slightly larger than the size of the porous electrode collector, so that the The edge extends beyond the edge of the porous electrode current collector, securing the edge of the separator over the edge of the porous electrode current collector. This method of flattening and fixing the coating (that is, edge-wrapping composite treatment) reduces the risk of burrs piercing the separator, especially when the coating is fixed by adhesive, which greatly improves the safety of the battery.

利用本发明的制备方法可以制备正极复合集流隔离层和负极复合集流隔离层。在正极复合集流隔离层中,多孔电极集流体为例如铝网的多孔正极集流体;在负极复合集流隔离层中,多孔电极集流体为例如铜网的多孔负极集流体。The preparation method of the present invention can be used to prepare the positive electrode composite current collecting and separating layer and the negative electrode composite current collecting and separating layer. In the positive electrode composite current collector separation layer, the porous electrode current collector is a porous positive electrode current collector such as aluminum mesh; in the negative electrode composite current collector separation layer, the porous electrode current collector is a porous negative electrode current collector such as copper mesh.

正极复合集流隔离层和负极复合集流隔离层可以用于锂浆料电池的电芯中。在锂浆料电池的电芯中,正极复合集流隔离层的隔膜与负极复合集流隔离层的隔膜相对放置,两层隔膜邻接。正极复合集流隔离层的多孔正极集流体的外侧设有多孔正极材料层,负极复合集流隔离层的多孔负极集流体的外侧设有多孔负极材料层。在多孔正极材料层的外侧设置另一正极复合集流隔离层,其中,正极复合集流隔离层的多孔正极集流体与多孔正极材料层邻接;在多孔负极材料层的外侧设置另一负极复合集流隔离层,其中,负极复合集流隔离层的多孔负极集流体与多孔负极材料层邻接。以该方式层叠形成锂浆料电池的电芯。多孔正极材料层和多孔负极材料层可以为粉末状、块状或浆料状等,由于在锂浆料电池中,注入电解液后,多孔正极材料层和多孔负极材料层在受到外力的情况下可以发生一定的变形,因此,当多孔正极材料层与正极复合集流隔离层的多孔正极集流体邻接时或者当多孔负极材料层与负极复合集流隔离层的多孔负极集流体邻接时,并不会将多孔正极集流体上的拱形部和多孔负极集流体上的拱形部完全压平,而是通过多孔正极材料层和多孔负极材料层的局部变形维持了拱形部的通道形状,从而在电芯中保留了可供电解液流动的流动通道。The positive electrode composite current collecting and separating layer and the negative electrode composite current collecting and separating layer can be used in batteries of lithium slurry batteries. In the battery cell of the lithium slurry battery, the diaphragm of the positive electrode composite current collecting and separating layer is placed opposite to the diaphragm of the negative electrode composite current collecting and separating layer, and the two layers of diaphragms are adjacent to each other. The outer side of the porous positive electrode current collector of the positive electrode composite current collection and separation layer is provided with a porous positive electrode material layer, and the outer side of the porous negative electrode current collector of the negative electrode composite current collection separation layer is provided with a porous negative electrode material layer. Another positive electrode composite current collector separation layer is set outside the porous positive electrode material layer, wherein the porous positive electrode current collector of the positive electrode composite current collector separation layer is adjacent to the porous positive electrode material layer; another negative electrode composite current collector is set outside the porous negative electrode material layer A current separation layer, wherein the porous negative electrode current collector of the negative electrode composite current collector separation layer is adjacent to the porous negative electrode material layer. In this manner, cells are stacked to form a lithium slurry battery. The porous positive electrode material layer and the porous negative electrode material layer can be in the form of powder, block or slurry, etc., because in the lithium slurry battery, after the electrolyte is injected, the porous positive electrode material layer and the porous negative electrode material layer are under the condition of external force Certain deformation can occur, therefore, when the porous positive electrode material layer is adjacent to the porous positive electrode current collector of the positive electrode composite current collecting and separating layer or when the porous negative electrode material layer is adjacent to the porous negative electrode collecting body of the negative electrode composite current collecting and separating layer, it does not The arched portion on the porous positive electrode current collector and the arched portion on the porous negative electrode current collector will be completely flattened, but the channel shape of the arched portion is maintained through the local deformation of the porous positive electrode material layer and the porous negative electrode material layer, thereby Flow channels for electrolyte flow are reserved in the cell.

在无液电芯中,多孔正极材料层中的非粘接固定的正极活性导电颗粒和/或多孔负极材料层中的非粘接固定的负极储锂导电颗粒的堆积孔隙率可大于5%并小于60%。在浸入电解液的情况下,非粘接固定的正极活性导电颗粒和/或非粘接固定的负极储锂导电颗粒能够在电解液中移动并分别形成正极浆料和/或负极浆料。正极活性导电颗粒占正极浆料的质量比可以为10%~90%、优选地为15%~80%,负极储锂导电颗粒占负极浆料的质量比可以为10%~90%、优选地为15%~80%。正极活性导电颗粒平均粒径可以为0.05μm~500μm,正极活性材料与导电剂的质量比可以为20~98:80~2;负极储锂导电颗粒平均粒径可以为0.05μm~500μm,负极储锂材料与导电剂的质量比可以为20~98:80~2。In the aneroid cell, the stacking porosity of the non-adhesive and fixed positive electrode active conductive particles in the porous positive electrode material layer and/or the non-bonded and fixed negative electrode lithium storage conductive particles in the porous negative electrode material layer can be greater than 5% and Less than 60%. In the case of immersion in the electrolyte, the non-adhesive and fixed positive electrode active conductive particles and/or the non-bonded and fixed negative electrode lithium storage conductive particles can move in the electrolyte and form positive electrode slurry and/or negative electrode slurry respectively. The mass ratio of positive electrode active conductive particles to positive electrode slurry can be 10% to 90%, preferably 15% to 80%, and the mass ratio of negative electrode lithium storage conductive particles to negative electrode slurry can be 10% to 90%, preferably 15% to 80%. The average particle size of positive electrode active conductive particles can be 0.05 μm to 500 μm, and the mass ratio of positive electrode active material to conductive agent can be 20 to 98:80 to 2; the average particle size of negative electrode lithium storage conductive particles can be 0.05 μm to 500 μm, and the negative electrode storage The mass ratio of the lithium material to the conductive agent may be 20-98:80-2.

在锂浆料电池的电芯中设置根据本发明的复合集流隔离层的情况下,当向电池内注入电解液时,电解液从电芯表面的由复合集流隔离层形成的拱形开口迅速进入复合集流隔离层的流动通道,进而经由复合集流隔离层的多孔电极集流体进入多孔电极材料层,快速浸润整个多孔电极材料层以便形成电极浆料。In the electric core of the lithium slurry battery, under the situation that the composite current collecting and separating layer according to the present invention is set, when the electrolyte is injected into the battery, the electrolyte will flow from the arched opening formed by the composite current collecting and separating layer on the surface of the electric core. Quickly enter the flow channel of the composite current collecting and separating layer, and then enter the porous electrode material layer through the porous electrode current collector of the composite collecting and separating layer, and quickly infiltrate the entire porous electrode material layer to form electrode slurry.

本发明的优势在于:The advantages of the present invention are:

1)在多孔电极集流体的拱形部的凹进部分与隔膜之间形成用于电解液的流动通道,有利于电解液快速浸润电极片内部;通道同时可以用于电芯使用过程中的散热排气,防止气泡等残留在电极片表面上影响电池正常的充放电反应;1) A flow channel for the electrolyte is formed between the concave part of the arched part of the porous electrode collector and the diaphragm, which is conducive to the rapid infiltration of the electrolyte inside the electrode sheet; the channel can also be used for heat dissipation during the use of the cell Exhaust to prevent bubbles and other residues on the surface of the electrode sheet from affecting the normal charge and discharge reaction of the battery;

2)在复合集流隔离层中,隔膜的边缘对多孔电极集流体进行包边复合处理,可以有效防止多孔电极集流体边缘的毛刺接触导致的电池短路;2) In the composite current collector isolation layer, the edge of the diaphragm wraps the porous electrode collector, which can effectively prevent the short circuit of the battery caused by the burr contact on the edge of the porous electrode collector;

3)在本发明中,可以根据需要灵活设置不锈钢丝的布置方式,根据极片尺寸增减不锈钢丝的数量,从而方便灵活地在电芯内形成可供电解液流通的流动通道。3) In the present invention, the arrangement of the stainless steel wires can be flexibly set according to the needs, and the number of stainless steel wires can be increased or decreased according to the size of the pole pieces, so as to conveniently and flexibly form a flow channel in the battery cell through which the electrolyte can circulate.

附图说明Description of drawings

图1(a)-1(d)为根据本发明的制备方法中的不锈钢丝布置的示意图;Fig. 1 (a)-1 (d) is the schematic diagram according to the stainless steel wire arrangement in the preparation method of the present invention;

图2(a)-2(d)为根据本发明的复合集流隔离层的制备方法的示意图;Fig. 2 (a)-2 (d) is the schematic diagram according to the preparation method of composite collector isolation layer of the present invention;

图3为根据本发明的制备方法制备的电芯。Fig. 3 is an electric core prepared according to the preparation method of the present invention.

附图标记列表:List of reference signs:

1、1a、1b——不锈钢丝1, 1a, 1b - stainless steel wire

2——多孔电极集流体2——Porous electrode current collector

2a——拱形部2a——arched part

2b——流动通道2b - Flow channel

3——正极复合集流隔离层3——Positive composite current collecting and separating layer

4——负极复合集流隔离层4——Negative compound current collecting and separating layer

5——多孔正极材料层5——Porous cathode material layer

6——多孔负极材料层6——Porous negative electrode material layer

7——隔膜7 - Diaphragm

具体实施方式Detailed ways

下面将结合附图,通过实施例对本发明做进一步说明。The present invention will be further described through embodiments below in conjunction with the accompanying drawings.

图1(a)-1(d)为根据本发明的制备方法中的不锈钢丝布置的示意图。在如图1(a)所示的实施方式中,两组不锈钢丝1分别平行设置,并且两组不锈钢丝1再相互交叉设置;在如图1(b)所示的实施方式中,多条不锈钢丝1以沿中心向外辐射的方式设置;在如图1(c)所示的实施方式中,多条不锈钢丝1不规则地交叉设置;在如图1(d)所示的实施方式中,在沿着极片长度的方向上,设置直径较大的不锈钢丝1a,在沿着极片宽度的方向上,设置直径较小的不锈钢丝1b,这样,即使在极片较长的方向上也可以实现快速注液。1(a)-1(d) are schematic diagrams of the arrangement of stainless steel wires in the preparation method according to the present invention. In the embodiment shown in Figure 1 (a), two groups of stainless steel wires 1 are arranged in parallel respectively, and the two groups of stainless steel wires 1 are mutually intersected again; In the embodiment shown in Figure 1 (b), multiple Stainless steel wire 1 is arranged in the mode that radiates outward along the center; In the embodiment shown in Fig. 1 (c), a plurality of stainless steel wires 1 are irregularly crossed; In the direction along the length of the pole piece, the stainless steel wire 1a with a larger diameter is set, and the stainless steel wire 1b with a smaller diameter is set along the direction along the width of the pole piece, so that even in the direction where the pole piece is longer Rapid liquid injection can also be realized on the top.

图2(a)-2(d)为根据本发明的复合集流隔离层的制备方法的示意图。首先,如图2(a)所示,将不锈钢丝1进行铺设,铺设的方式可以根据实际需要设计;然后,如图2(b)所示,将多孔电极集流体2置于不锈钢丝1的上面,至少部分不锈钢丝1从多孔电极集流体2的边缘向外伸出。采用压力机对多孔电极集流体2进行加热加压处理,压力可以为5MPa,温度可以为120℃,使得多孔电极集流体2在与不锈钢丝1接触的位置处弯曲变形,形成包覆不锈钢丝1的拱形部;如图2(c)所示,在压制后的多孔电极集流体2上生成一面凹进、一面凸起的拱形部2a,拱形部2a的内径与不锈钢丝的外径大致相同;最后,如图2(d)所示,在多孔电极集流体2的拱形部2a凹进的一面上,将多孔电极集流体2的平面部分与隔膜7粘接,在多孔电极集流体2的拱形部2a的凹进部分与隔膜7之间形成用于电解液流通的流动通道2b,隔膜7的边缘对多孔电极集流体2进行包边复合处理。2(a)-2(d) are schematic diagrams of the preparation method of the composite current collecting and separating layer according to the present invention. First, as shown in Figure 2(a), the stainless steel wire 1 is laid, and the way of laying can be designed according to actual needs; then, as shown in Figure 2(b), the porous electrode current collector 2 is placed on the stainless steel wire 1 Above, at least part of the stainless steel wire 1 protrudes outward from the edge of the porous electrode current collector 2 . Use a press to heat and press the porous electrode current collector 2, the pressure can be 5MPa, and the temperature can be 120°C, so that the porous electrode current collector 2 is bent and deformed at the position in contact with the stainless steel wire 1 to form a coated stainless steel wire 1 The arched portion; as shown in Figure 2 (c), on the porous electrode current collector 2 after pressing, generate one side concave, one side convex arched portion 2a, the inner diameter of the arched portion 2a is the same as the outer diameter of the stainless steel wire Roughly the same; finally, as shown in Figure 2(d), on the concave side of the arched part 2a of the porous electrode current collector 2, the planar part of the porous electrode current collector 2 is bonded to the separator 7, and the porous electrode current collector A flow channel 2b for electrolyte circulation is formed between the recessed part of the arched part 2a of the fluid 2 and the diaphragm 7, and the edge of the diaphragm 7 performs edge wrapping composite treatment on the porous electrode current collector 2.

图3为根据本发明的制备方法制备的电芯。根据本发明的复合集流隔离层的制备方法制备正极复合集流隔离层3和负极复合集流隔离层4。在正极复合集流隔离层3中,多孔正极集流体为铝网,在负极复合集流隔离层4中,多孔负极集流体为铜网。在制备电芯时,两个正极复合集流隔离层3之间设置多孔正极材料层5,正极复合集流隔离层3的多孔正极集流体的拱形部的凸起一面与多孔正极材料层5邻接,两个负极复合集流隔离层4之间设置多孔负极材料层6,负极复合集流隔离层4的多孔负极集流体的拱形部的凸起一面与多孔负极材料层6邻接,正极复合集流隔离层3的隔膜与负极复合集流隔离层4的隔膜相邻,以此层叠形成电芯。Fig. 3 is an electric core prepared according to the preparation method of the present invention. According to the preparation method of the composite current collecting and separating layer of the present invention, the positive electrode composite current collecting and separating layer 3 and the negative electrode composite current collecting and separating layer 4 are prepared. In the positive electrode composite current collecting and separating layer 3 , the porous positive electrode current collector is an aluminum mesh, and in the negative electrode composite collecting and separating layer 4 , the porous negative electrode current collector is a copper mesh. When preparing the electric core, a porous positive electrode material layer 5 is arranged between the two positive electrode composite current collector separation layers 3, and the convex side of the arched part of the porous positive electrode current collector of the positive electrode composite current collector separation layer 3 and the porous positive electrode material layer 5 Adjacent, a porous negative electrode material layer 6 is set between the two negative electrode composite current collector separation layers 4, and the convex side of the arched part of the porous negative electrode current collector of the negative electrode composite current collector separation layer 4 is adjacent to the porous negative electrode material layer 6, and the positive electrode composite The diaphragm of the current collecting and separating layer 3 is adjacent to the diaphragm of the negative electrode compound current collecting and separating layer 4, so as to be stacked to form an electric core.

当向电池内注入电解液时,在电芯的表面上,电解液经由多孔电极集流体的边缘所形成的拱形开口进入复合集流隔离层的流动通道2b,流动通道2b内的电解液可以浸润隔膜并且可以穿过多孔电极集流体浸润多孔电极材料层,从而达到整个电芯快速浸润的目的。When the electrolyte is injected into the battery, on the surface of the battery cell, the electrolyte enters the flow channel 2b of the composite collector separation layer through the arched opening formed by the edge of the porous electrode collector, and the electrolyte in the flow channel 2b can be Wetting the separator and wetting the porous electrode material layer through the porous electrode current collector, so as to achieve the purpose of rapid wetting of the entire battery cell.

本发明具体实施例并非用以限定本发明。任何熟悉本领域的技术人员,在不脱离本发明技术方案范围情况下,都可利用上述揭示的方法和技术内容对本发明技术方案作出许多可能的变动和修饰,或修改为等同变化的等效实施例。因此,凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所做的任何简单修改、等同变化及修饰,均仍属于本发明技术方案保护的范围内。The specific embodiments of the present invention are not intended to limit the present invention. Any person familiar with the art, without departing from the scope of the technical solution of the present invention, can use the methods and technical content disclosed above to make many possible changes and modifications to the technical solution of the present invention, or modify it into an equivalent implementation of equivalent changes example. Therefore, any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention, which do not deviate from the technical solution of the present invention, still fall within the protection scope of the technical solution of the present invention.

Claims (8)

1.一种复合集流隔离层的制备方法,其特征在于,所述制备方法包括如下步骤:(a)在多孔电极集流体的下方铺设多条不锈钢丝,至少部分不锈钢丝的端部延伸超出所述多孔电极集流体的边缘;(b)采用压力机对所述多孔电极集流体进行加热加压处理,所述多孔电极集流体在与所述不锈钢丝接触的部位弯曲变形,从而在所述多孔电极集流体上形成一面凹进并且一面凸起的弯折部;(c)在所述多孔电极集流体的弯折部的凹进的一面上,所述多孔电极集流体的平面部分与隔膜复合,所述多孔电极集流体的弯折部的凹进部分与所述隔膜之间形成流动通道,所述隔膜的边缘对所述多孔电极集流体进行包边复合处理。1. A preparation method of a composite current collecting and separating layer, characterized in that, the preparation method comprises the steps of: (a) laying a plurality of stainless steel wires under the porous electrode current collector, at least the ends of some stainless steel wires extend beyond The edge of the porous electrode current collector; (b) heat and pressurize the porous electrode current collector with a press, and the porous electrode current collector is bent and deformed at the part in contact with the stainless steel wire, so that A bent portion with one side concave and one side convex is formed on the porous electrode current collector; (c) on the concave side of the bent portion of the porous electrode current collector, the planar part of the porous electrode current collector and the diaphragm Composite, a flow channel is formed between the recessed part of the bent part of the porous electrode collector and the separator, and the edge of the separator performs edge-wrapping composite treatment on the porous electrode collector. 2.根据权利要求1所述的制备方法,其中,所述多孔电极集流体为多孔正极集流体,所述多孔正极集流体为具有通孔结构的厚度为1μm~2000μm的电子导电层,所述多孔正极集流体的孔径为0.01μm~2000μm,通孔孔隙率可以为10%~90%,所述多孔正极集流体为导电金属层,所述导电金属层为金属网或金属丝编织网;或者,所述导电金属层为具有通孔结构的泡沫金属网;或者,所述导电金属层为多孔金属板或多孔金属箔,所述导电金属层的材料为铝。2. The preparation method according to claim 1, wherein the porous electrode current collector is a porous positive electrode current collector, and the porous positive electrode current collector is an electronically conductive layer having a through-hole structure with a thickness of 1 μm to 2000 μm, the The pore diameter of the porous positive current collector is 0.01 μm to 2000 μm, and the porosity of the through holes can be 10% to 90%. The porous positive current collector is a conductive metal layer, and the conductive metal layer is a metal mesh or a wire woven mesh; or , the conductive metal layer is a foamed metal mesh with a through-hole structure; or, the conductive metal layer is a porous metal plate or a porous metal foil, and the material of the conductive metal layer is aluminum. 3.根据权利要求1所述的制备方法,其中,所述多孔电极集流体为多孔负极集流体,所述多孔负极集流体为具有通孔结构的厚度为1μm~2000μm的电子导电层,所述多孔负极集流体的孔径为0.01μm~2000μm,通孔孔隙率可以为10%~90%,所述多孔负极集流体为导电金属层,所述导电金属层为金属网或金属丝编织网;或者,所述导电金属层为具有通孔结构的泡沫金属网;或者,所述导电金属层为多孔金属板或多孔金属箔,所述导电金属层的材料为铜。3. The preparation method according to claim 1, wherein the porous electrode current collector is a porous negative electrode current collector, and the porous negative electrode current collector is an electronically conductive layer having a through-hole structure with a thickness of 1 μm to 2000 μm, the The pore diameter of the porous negative electrode current collector is 0.01 μm to 2000 μm, and the porosity of the through holes can be 10% to 90%. The porous negative electrode current collector is a conductive metal layer, and the conductive metal layer is a metal mesh or a wire woven mesh; or , the conductive metal layer is a foamed metal mesh with a through-hole structure; or, the conductive metal layer is a porous metal plate or a porous metal foil, and the material of the conductive metal layer is copper. 4.根据权利要求1所述的制备方法,其中,在步骤(a)中,所述多条不锈钢丝交叉铺设,从而在所述多孔电极集流体上形成相互交叉连通的通道。4. The preparation method according to claim 1, wherein, in step (a), the plurality of stainless steel wires are laid crosswise, so as to form mutually cross-connected channels on the porous electrode current collector. 5.根据权利要求1所述的制备方法,其中,在步骤(a)中,所述不锈钢丝的直径为0.5~5mm。5. The preparation method according to claim 1, wherein, in step (a), the diameter of the stainless steel wire is 0.5-5mm. 6.根据权利要求1所述的制备方法,其中,在步骤(b)中,加热温度为50~200℃。6. The preparation method according to claim 1, wherein, in step (b), the heating temperature is 50-200°C. 7.根据权利要求1所述的制备方法,其中,在步骤(b)中,加压压力为2~20MPa。7. The preparation method according to claim 1, wherein, in step (b), the applied pressure is 2-20 MPa. 8.根据权利要求1所述的制备方法,其中,在步骤(c)中,所述多孔电极集流体的平面部分与所述隔膜复合的方式包括粘接或平面热压复合。8 . The preparation method according to claim 1 , wherein, in step (c), the planar part of the porous electrode current collector is combined with the separator by bonding or planar thermocompression.
CN202111232547.0A 2021-10-22 2021-10-22 A kind of preparation method of composite current collecting and separating layer Pending CN116014363A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117477049A (en) * 2023-12-28 2024-01-30 北京希倍动力科技有限公司 Battery capable of absorbing and dredging gas and battery cell comprising same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117477049A (en) * 2023-12-28 2024-01-30 北京希倍动力科技有限公司 Battery capable of absorbing and dredging gas and battery cell comprising same
CN117477049B (en) * 2023-12-28 2024-08-27 北京希倍动力科技有限公司 Battery capable of absorbing and dredging gas and battery cell comprising same

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