Patent Application
20220029143
The present invention relates to a method.
Because of their high energy density and their good thermal stability, secondary batteries, preferably lithium ion batteries, are suitable for the storage of electrical energy in various application fields, above all in electrically powered vehicles.
Lithium ion batteries comprise one or more lithium ion battery cells. Such lithium ion battery cells conventionally contain one or more electrode units in the form of electrode windings or electrode stacks, which have at least one positive electrode, at least one negative electrode and at least one ion-conducting separator that spatially separates the positive and negative electrodes from one another. The positive and negative electrodes are respectively located at a positive and negative current collector. When forming a lithium ion battery cell, the electrode units are accommodated in a housing, which may be prismatic, round or foil-like, depending on the application.
The properties characterizing the lithium ion battery cells, such as electrical conductivity, power density and energy density, are primarily dependent on the design and material properties as well as the production process of the positive electrode.
In this regard, a method for producing a positive electrode, in which a mixture of an active material having a multiplicity of active material particles and a conductive additive is provided in a first method step, is known from US 2017/8468 A1. The active material particles preferably have a mean diameter of from 10 to 50 nm.
A further method for producing a positive electrode for a lithium ion battery cell, in which a mixture of active material and a conductive additive is provided in a first method step, the active material preferably having larger particles than the conductive additive, is known from US 2017/098817 A1.
According to the invention, a method for producing a positive electrode for a battery cell is provided, the positive electrode comprising an active material and a conductive additive.
The active material contains a first number of active material particles, in particular spherical active material particles, which have a first mean diameter. A second number of conductive additive particles, in particular spherical conductive additive particles, is at the same time provided. The conductive additive particles have a second mean diameter. Active material refers to those material components of an electrode at which the corresponding electrochemical processes, for example the intercalation or deintercalation of lithium ions, take place during operation of the battery cell.
The conductive additive is used to increase the electrical conductivity in the positive electrode and to electrically connect individual active material particles to one another.
In a first method step, the active material and the conductive additive are provided, the number of conductive additive particles being adjusted according to a ratio of the second mean diameter to the first mean diameter and the number of active material particles.
In this case, it is advantageous that a surface of the active material particles is coated surface-wide with conductive additive material particles. As a result of the above-described setting of the number of conductive additive particles, the surface of the active material particles is covered substantially fully by the conductive additive particles provided. The total electrical resistance of the battery cell, comprising an ohmic resistance, a charge transfer resistance and a diffusion resistance, is thus reduced significantly in comparison with conventional battery cells.
The dependent claims relate to further advantageous embodiments of the present invention.
Thus, it is advantageous for conductive additive particles to be dispersed in a binder in a second method step.
It is furthermore advantageous for an initial weight of the binder to be adjusted in the second method step to be equal to an initial weight of the conductive additive particles provided in the first method step.
It is furthermore advantageous for the dispersion of the binder and the conductive additive particles to be mixed in a third method step with the active material particles that are provided in the first method step.
In order to reduce the diffusion resistance which is caused by movement of the lithium ions between a positive and negative electrode in a battery cell, preferably in a lithium ion battery cell, a further quantity of binder is mixed with a further quantity of conductive additive particles in a fourth method step. The total quantity of conductive additive particles in the positive electrode is preferably from 4% to 10% in relation to the total quantity of active material particles. The total quantity of conductive additive particles is made up of a quantity according to the first method step and a further quantity according to the third method step.
In a fifth method step, the mixture comprising binder and conductive additive particles from the fourth method step is mixed with the mixture from the third method step.
It is in this case advantageous for a solvent to be added in a sixth method step to the mixture according to the fifth method step, in order to be able to suspend all the solids, in particular the binder. The solvent may be N-methyl-2-pyrrolidone (NMP).
When forming a positive electrode layer, the suspension according to the sixth method step is applied on a carrier foil in a seventh method step. The carrier foil preferably comprises an aluminum foil, which also functions as a positive current collector. After the application of the suspension on the carrier foil, the solvent is finally evaporated, for example in an autoclave.
The method according to the invention may advantageously be used for positive electrodes in lithium ion battery cells that are employed in electrical vehicles, in hybrid vehicles, or in static applications, for example for the storage of regeneratively obtained energy.
Advantageous embodiments of the present invention are represented in the drawing and explained in more detail in the following description of the figures.
In a first method step 102, an active material and a conductive additive are provided. Preferably, the active material may be a lithium metal oxide, a lithium iron phosphate or a lithium titanate oxide, and the conductive additive may comprise carbon black.
The active material has a first number n1 of active material particles, in particular spherical active material particles. Furthermore, the conductive additive has a second number n2 of conductive additive particles, in particular spherical conductive additive particles. There is a first mean diameter
where N stands for a number in a range of 1.6 and 1.7. Preferably, N is equal to 1.64.
In a second method step 104, the conductive additive particles according to the first method step are dispersed in a binder. The binder may for example comprise a polymer, preferably polyvinylidene fluoride (PVDF). An initial weight of the binder is in this case adjusted in such a way that the initial weight of the binder is equal to an initial weight of the conductive additive particles.
Next, the dispersion is mixed in a third method step 106 with the active material particles which are provided according to the first method step 102.
In a fourth method step 108, a further quantity of binder is then mixed with a further quantity of conductive additive particles.
Subsequently, in a fifth method step 110, the mixture of the further quantity of binder and the further quantity of conductive additive particles is combined with the mixture according to the third method step 106.
Next, in a sixth method step 112, the mixture according to the fifth method step 110 is suspended in a solvent, preferably N-methyl-2-pyrrolidone (NMP). This suspension is applied on a carrier foil in a seventh method step 114. This carrier foil may be an aluminum foil, which also functions as a positive current collector for the positive electrode.
Finally, in an eighth method step 116, the solvent of the suspension is evaporated. This process may preferably be carried out in an autoclave at a temperature of from 140° C. to 160° C.
Such positive electrodes 20 may advantageously be used for battery cells that are employed in motor vehicles, particularly in electric vehicles (EV), hybrid (electric) vehicles (HEV) and plug-in hybrid (electric) vehicles (PHEV).
| Number | Date | Country | Kind |
|---|---|---|---|
| 10 2018 219 472.6 | Nov 2018 | DE | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2019/080854 | 11/11/2019 | WO | 00 |
