CN-122025506-A - Method for producing electrode mixtures and dry electrodes by means of a cooling container

Abstract

The application relates to a method for producing electrode mixtures and dry electrodes by means of a cooling container. The application relates to a method for producing and preparing an electrode mixture from an active material, optionally additives and a binder, comprising the steps of 1) producing the electrode mixture in a mixing vessel of a mixer, wherein the mixture is heated to a temperature T H during production, wherein T H >45 ℃, 2) transferring the electrode mixture into a cooling mixer with a cooling vessel, the walls of which are preferably cooled, 3) cooling the electrode mixture in the cooling vessel to a removal temperature T E , which is preferably <35 ℃, 4) removing the electrode mixture from the cooling vessel. The application also relates to a method for producing a dry electrode from an electrode mixture.

Inventors

• Stephen Gael

Assignees

• 德国古斯塔夫·爱立许机械制造有限公司

Dates

Publication Date

20260512

Application Date

20250307

Priority Date

20241111

Claims (10)

1. 1. A method for preparing and conditioning an electrode mixture comprised of an active material, optional additives and a binder, the method comprising the steps of: 1) Preparing the electrode mixture in a mixing vessel of a mixer, wherein the mixture is heated to a temperature T H during the preparation, wherein T H >45 ℃, 2) Transferring the electrode mixture into a cooling mixer having a cooling vessel, the walls of which are preferably cooled, 3) Cooling the electrode mixture in the cooling vessel to a withdrawal temperature T E , preferably < 35C, 4) The electrode mixture is removed from the cooling vessel.
2. 2. Method according to claim 1, characterized in that in step 3) the electrode mixture is cooled to at least 9 ℃, preferably to a removal temperature T E <19 ℃, wherein preferably dry ice or liquid gas is introduced into the cooling vessel.
3. 3. Method according to claim 1, characterized in that in step 3) cooling is performed to not lower than the withdrawal temperature T E >24 ℃, and after step 4) the electrode mixture is supplied to a cooling device, by means of which the electrode mixture is cooled to at least 4 ℃, preferably to a temperature T K <19 ℃.
4. 4. A method according to claim 3, characterized in that a transfer line of a pneumatic transfer device for removing the electrode mixture from the cooling vessel is provided as a cooling device, which transfer line is operated with a gas, preferably having a temperature T G <19 ℃, wherein dry ice or liquid gas is preferably introduced into the cooling vessel in step 3), between steps 3) and 4) and/or during step 4), and the gas produced by sublimation or evaporation is led into the transfer line.
5. 5. Method according to claim 3 or 4, characterized in that the electrode mixture after step 4) is transferred into a buffer container, wherein preferably the buffer container is temperature-adjustable and serves as a cooling device, wherein the buffer container is preferably implemented with double walls, wherein a cooling fluid can flow between the two walls, and/or the buffer container has an insulating device, wherein particularly preferably the electrode mixture moves in the buffer container.
6. 6. Method according to any of claims 2 to 5, characterized in that the electrode mixture after step 4) is applied to a sieving device and only undersize is used as modulated electrode mixture, wherein preferably the sieving device has a mesh width of less than 10mm, particularly preferably less than 5mm, most preferably less than 2mm.
7. 7. The method of claim 6, wherein oversize is directed into the vessel, the cooling vessel, the buffer vessel, a comminution device, or the transfer line.
8. 8. Method according to claim 6, characterized in that a friction screening device or particularly preferably a vortex screening device is used as screening device, wherein preferably the use is made in such a way that no oversize remains.
9. 9. A method of manufacturing a dry electrode from an electrode mixture prepared by means of the method according to any of the preceding claims, It is characterized in that the method comprises the steps of, The electrode mixture is supplied to a calender and calendered into a web, wherein the edge strips or excess material of the web are subsequently separated to ensure a uniform width of the web, and the separated edge strips or excess material is directed into the container, the cooling mixer, the buffer container or the transfer line.
10. 10. A method according to claim 9, characterized in that comminuting means are provided for dividing the separated edge strip into smaller strip sections.

Description

Method for producing electrode mixtures and dry electrodes by means of a cooling container The present invention relates to a method of preparing and conditioning a dry electrode mixture. The invention also relates to a method for producing dry electrodes from these electrode mixtures. In recent years, battery technology, in particular lithium ion technology, has become a focus of attention, as this technology is critical for the function of, for example, fully electrically driven vehicles, but also for stationary power storages. The low cost of manufacturing a high capacity durable battery is a prerequisite for acceptance of all-electric drive vehicles. Currently, lithium ion batteries are mainly used. In this category, there are several specific battery chemistries that predominate, with the most widely used cathode materials being as follows: nickel Manganese Cobalt (NMC) electrode mixtures-these cells use mixtures consisting of nickel, manganese and cobalt. Nickel provides a high energy density, manganese provides thermal stability, and cobalt is responsible for stabilizing the structure. Nickel Cobalt Aluminium (NCA) electrode mixtures containing nickel, cobalt and aluminium in the cathode. The aluminum content stabilizes the structure and increases the service life, while nickel maximizes the energy density. Lithium iron phosphate (LFP) electrode mixtures in which lithium iron phosphate is used as cathode material in such cobalt-free battery chemistries, which have lower energy densities but provide longer service life and better thermal stability. The anode is typically composed of graphite or a silicon-graphite mixture. In all of these types, the electrode mixture is prepared using a polymeric binder (partially with a conductive additive as well), applied to a discharge foil (Ableitfolie), and calendered during or after this to optimize the structural integrity and density of the electrode. In addition, there are some advances that may play a relevant role in the future. In addition to the lower cost but less performing and cobalt-free sodium ion battery chemistries, all-solid state batteries with solid state electrolytes are being actively developed. Theoretically, this technique provides a higher energy density than conventional lithium ion batteries, and also provides higher safety since the electrolyte is solid. The fabrication of all of these cells is expected to continue to require calendaring of the electrodes, which can present various challenges to the calendaring process. In summary, calendaring of electrode mixtures will also play an important role in future battery technology, as calendaring optimizes the density, uniformity and mechanical properties of the electrodes. However, the specific materials used depend on advances in materials science and the requirements of electric vehicles. Typical lithium ion battery electrodes have copper foil serving as an anode and aluminum foil serving as a cathode. These foils are typically coated on both sides with an active material and also with additives at least for the purpose of manufacturing the cathode. High demands are placed on the electrodes in order to be able to produce reliable high-capacity lithium ion batteries. The electrode layer needs to have a defined constant thickness and a defined pore structure into which electrolyte can enter in order to be able to transport lithium ions to each particle of the active material. In an ideal case, the active material needs to be impregnated with the electrolyte as large an area as possible. Furthermore, the active material particles need to be electrically connected to the metal foil (i.e., to the copper foil or aluminum foil in the example) to ensure that electrons are transported to and from each active material particle. In addition, the active material particles need to be bonded to each other and to the metal foil, for which purpose a binder material is used. Finally, the layer thickness should be formed as uniformly as possible over the width and length. In order to manufacture these layers, the raw materials (i.e. active material, binder and optional additives) need to be mixed with each other and dispersed into a so-called "slurry (paste, suspension)". Typically, a liquid solvent (e.g., water or N-methyl-2-pyrrolidone (NMP)) is added here, which needs to be removed again by a complicated drying process after application of the electrode mixture to the foil. The cavities created during the drying process are compressed into a defined porosity during the subsequent calendering process. Mainstream electrode wet processing is both time and energy consuming. Furthermore, in the machine production of electrode mixtures, it is often necessary to provide a bulky drying device. There are also methods for dry preparation of electrode mixtures, i.e. using little or even no solvent at all. In this case, however, when the components are mixed, a more intensive treatment is required in order to conver