Patent Application
20140030596
Embodiments of the present invention relate to a cathode for a sodium-metal halide battery, a sodium-metal halide battery comprising the same, methods for preparing the cathode and the battery, and use of the battery.
The sodium-metal halide battery appeared in the 1990's as a new generation of high temperature rechargeable batteries. Due to its large energy density, high cycle life, improved safety, and high temperature stability, it can be used in various applications such as hybrid vehicles, uninterruptable power supply, and the like.
In the present sodium-metal halide battery, a mixture of active materials is loaded in the form of millimeter-scale granules, and metal powders inside the granules form a foam-like network to conduct electronic current. For example, in some of the contemplated designs for sodium-nickel halide battery cells, the cathode grid is formed from various types of nickel powder. Based on the volume inside the granules, the volume fraction of the conductive material Ni is about 20-30%, which is enough to reach a percolation threshold. However, since the material forming the granules only accounts for about 50% of the total volume of the cathode, the average volume fraction of the conductive material in the cathode is about 10-15%. Ni migrates with repeated cycling of the battery, which causes the cathode electronic conductivity to degrade. Consequently, the internal resistance of the battery cell increases.
It is well known that low internal resistance is critical for high battery discharge power, which is an important requirement for high power applications. It can be seen from the above that sodium-metal halide batteries may still sometimes exhibit problems with cycling-induced increased internal resistance, and thus deteriorated discharge power. Moreover, there is a need for increased initial discharge power performance.
Thus, some of the sodium-metal halide batteries can continue to benefit from improvements in certain aspects and characteristics.
An object of embodiments of the present invention is to improve conductivity of a cathode for a sodium-metal halide battery, thereby decreasing internal resistance of the battery and improving battery discharge power.
According to an embodiment of the present invention, a cathode for a sodium-metal halide battery is provided, wherein the cathode contains a metal microwire, that is, the cathode comprises the metal microwire.
According to an embodiment of the present invention, a sodium-metal halide battery is provided. The sodium-metal halide battery compries: a cathode, comprising a metal microwire; an anode; and an electrolyte.
According to an embodiment of the present invention, a method for preparing the cathode comprising a metal microwire for a sodium-metal halide battery is provided, wherein the metal microwire is added during a granulation process of active material and/or a cathode filling process.
According to an embodiment, a method for preparing a sodium-metal halide battery is provided, wherein the sodium-metal halide battery contains a cathode comprising a metal microwire, and wherein the metal microwire is added during a granulation process of active material and/or during a cathode filling process.
According to an embodiment of the present invention, use of the sodium-metal halide battery as an uninterruptable power supply is provided.
These and other advantages and features will be more readily understood from the following detailed description of embodiments of the present invention, which are provided in connection with the accompanying drawings.
a is a top view illustrating a portion of the structure of a sodium-metal halide battery according to an embodiment of the present invention.
b is a side view illustrating a portion of the structure of the sodium-metal halide battery according to an embodiment of the present invention.
According to an embodiment of the present invention a cathode for a sodium-metal halide battery is provided. A metal microwire is added into the cathode for a sodium-metal halide battery of an embodiment of the present invention. The metal microwire reinforces the electronically conducting cathode grid, and thus improves the electronic conductivity of the cathode, and the stability of its conductive network, thereby decreasing internal resistance of the battery cell, and improving the discharge power of the battery. In addition, use of the microwire can potentially extend the battery lifetime.
The metal or metal alloy for the microwire used in the cathode of an embodiment of the present invention is electrochemically stable. In particular, no redox reaction occurs on said metal or metal alloy of metal microwire in the voltage range of charging and discharging of said battery. However, in those cases in which a redox rection does occur, it is usually a reversible reaction. Such a reaction should be confined to a minor portion of the microwire. That is, when the metal microwire is oxidized to a certain depth, the dynamic process of the electrochemical oxidation reaction is slow enough to be negligible. The electrochemical reaction is limited by surface passivation, much like aluminum stops oxidizing after a thin aluminum oxide film forms on the surface. In this way, the metal microwire will not be completely dissolved with cycling of the battery so that the conductivity of the cathode is improved. The resistivity of the metal of metal microwire is 10−6 Ω·cm or less. Exemplary microwire metals include at least one selected from the group consisting of nickel, molybdenum, and tungsten, but are not limited thereto.
In an embodiment of the present invention, the metal microwire has an aspect ratio of greater than 10 and less than or equal to 100. According to another embodiment, the metal microwire has an aspect ratio of greater than 20 and less than or equal to 100. In an embodiment of the present invention, the metal microwire has a diameter of 1 micron to 1 millimeter. In another embodiment, the metal microwire has a diameter of 1 micron to 200 microns. In another embodiment, the metal microwire has a diameter of 1 micron to 100 microns. In yet another embodiment the metal microwire has a diameter of 10 to 100 microns. In an embodiment of the present invention, the length of the metal microwire a length of 1 mm to 20 mm. According to another embodiment the metal microwire has a length of 1 mm to 10 mm.
For example, the metal microwire used in examples of the present invention can be a nickel fibre having a diameter of less than 100 microns and a length of 1 mm to 3 mm. Its micrograph is shown in
In an embodiment of the present invention, a volume fraction of the metal microwire is greater than a percolation threshold. When the volume fraction of the metal microwire is greater than the percolation threshold, a continuous conductive network can be built, thereby further improving the conductivity of the cathode. The percolation threshold is a value based on a percolation theory. It can be calculated though mathematical model, or can be measured by experiment. For example, reference can be made to E. J. Garboczi, K. A. Snyder, J. F. Douglas, Geometrical percolation threshold of overlapping ellipsoids, Physical Review E, Volume 52, Number 1.
In an embodiment of the present invention, the metal microwire can be inter-granular of active cathode material and/or intra-granular of active cathode material when the active material has been granulated. In particular, if the metal microwire and the active material are mixed together to be granulated during the granulation process of active material, the metal microwire is intra-granular of active material. If the metal microwire is added to the granules of active material during a cathode filling process, after the granulation process of active material, the metal microwire is inter-granular of active material.
The active material used in the cathode of embodiments of the present invention can be any active material commonly used in the field. The active material includes nickel powder, sodium chloride and other additive(s). For example, the active material may include: 40 to 70 wt % of nickel (Ni) powder, 30 to 50 wt % of sodium chloride (NaCl), 0.1 to 5 wt % of sodium fluoride (NaF), 0.1 to 5 wt % of aluminum (Al) powder, 0.1 to 1 wt % of sodium iodide (NaI), 0 to 20 wt % of iron (Fe) powder, 0 to 10 wt % of zinc sulfide (ZnS), and 0 to 10 wt % of iron (II) sulfide (FeS).
The cathode according to an embodiment of the present invention can further include a catholyte. The catholyte can be any catholyte commonly used in the field, such as NaAlCl4.
According to an embodiment of the present invention, a method for preparing the cathode for a sodium-metal halide battery cell is provided. The method for preparing the cathode according to an embodiment of the present invention is the same as a method for preparing a cathode commonly used in the field, except that a metal microwire is added during a granulation process of active material and/or during a cathode filling process. When it is desired that the metal microwire is intra-granular of active material, the metal microwire and the active material are mixed together to be granulated during the granulation process. When it is desired that the metal microwire is inter-granular of active material, the metal microwire is added to be mixed with the granules of active material during the cathode filling process after granulation of the active material, and then the mixture is poured into a cathode compartment. When it is desired that the metal microwire is both inter-granular of active material and intra-granular of active material, both steps described above are carried out.
According to an embodiment of the present invention a sodium-metal halide battery that contains a cathode is provided. The structure of the sodium-metal halide battery according to an embodiment of the present invention is described below by referring to
By referring to
In the sodium-metal halide battery cell according to an embodiment of the present invention, a cathode compartment is separated from an anode compartment by the ceramic electrolyte 3, wherein the cathode compartment is inside the ceramic electrolyte 3, and the anode compartment is between the ceramic electrolyte 3 and the case 5. The ceramic electrolyte 3 can be any ceramic electrolyte commonly used in the field, such as β-alumina.
The cathode 1 is accommodated in the cathode compartment. In the cathode 1, granules of active material (for example, nickel and sodium chloride) are impregnated or otherwise incorporated into a catholyte such as molten NaAlCl4. A metal microwire is added to the cathode 1. The metal microwire can be inter-granular of active material and/or intra-granules of active material.
The anode 2 is accommodated (incorporated into) in the anode compartment. The anode 2 can be a sodium metal.
The cathode current collector 4 is also accommodated in the cathode compartment. The cathode current collector 4 can be any cathode current collector commonly used in the field, such as Ni.
The case 5 can be any case commonly used in the field. For example, the case 5 can be made of steel. The steel can be mild steel.
The shim 6 when present is used to ensure that the liquid level of sodium metal in the anode is equivalent to the level of active material in the cathode. The shim 6 can be made by any material commonly used in the field, such as mild steel.
The carbon fiber wick 7 is used to transport an electrolyte solution.
The cell filling port 8 is used to fill the granules of active material and the catholyte into the cathode compartment.
The sealing system 9 is used to seal the cathode and the anode from each other and from the external environment, while maintaining electronic isolation between the cathode and the anode. The sealing system 9 can be comprised of materials commonly used in the field, such as α-Al2O3, nickel and silica glass.
According to an embodiment of the present invention a method for preparing the sodium-metal halide battery cell is provided. The method for preparing the battery cell according to an embodiment of the present invention is the same as a method for preparing a battery cell commonly used in the field, except that during preparation of a cathode, as described above, a metal microwire is added during a granulation process of active material and/or a cathode filling process. Regarding other steps in the method for preparing the sodium-metal halide battery, they are the same as those commonly used in the field. Therefore, the detailed description is omitted herein.
An embodiment of the present invention also relates to the use of the sodium-metal halide battery, for example in an unintermptable power supply
Embodiments of the present invention are further described by reference to examples below. However, the examples are only exemplary, and not limiting of the present invention.
A cathode is prepared by granulating 220 to 240 g of active material to obtain granules of active material, uniformly mixing the granules of active material with 20 g of nickel microwire (diameter: 25 microns, length: 1 millimeter) as a metal microwire, adding the mixture of the granules of active material and the nickel microwire into a cathode compartment, and adding 110 to 120 g of NaAlCl4 as a catholyte into the cathode compartment. The active material includes: 40 to 70 wt % of nickel (Ni) powder, 30 to 50 wt % of sodium chloride (NaCl), 0.1 to 5 wt % of sodium fluoride (NaF), 0.1 to 5 wt % of aluminum (Al) powder, 0.1 to 1 wt % of sodium iodide (NaI), 0 to 20 wt % of iron (Fe) powder, 0 to 10 wt % of zinc sulfide (ZnS), and 0 to 10 wt % of iron (II) sulfide (FeS).
The anode compartment need not initially contain sodium metal, since the sodium metal will be produced during charging of the cell. The cathode and the anode are separated by β-alumina as a ceramic electrolyte. A cathode current collector is a U-shaped nickel rod having a diameter of 3.0 to 4.0 mm. A sodium-nickel chloride battery is manufactured from the above cathode, anode, cathode current collector, and ceramic electrolyte by a common method in the field.
A sodium-nickel chloride cell is manufactured in the same manner as in Example 1, except that the granules of active material are mixed with 30 g of nickel microwire as a metal microwire.
A sodium-nickel chloride cell is manufactured in the same manner as in Example 1, except that no metal microwire is added.
The performance of the sodium-nickel chloride cells manufactured according to Examples 1 and 2 and Comparative Example are evaluated by using an electrochemical cycling testing machine (Digatron) as follows: respectively discharging at constant temperature of 300° C., and at a constant power of 120, 130, 140, and 155 W, until the voltage reaches 1.8V or after 15 minutes. The results are shown in
It can be seen from
The metal microwire builds a secondary grid other than a cathode grid, and thus improves the cathode conductivity and the stability of its conductive network, thereby decreasing internal resistance of the battery and improving discharge power of the battery.
While the invention has been described in detail in connection with particular embodiments, it should be understood that the invention is not limited to such disclosed embodiments. Rather, the invention can be modified to incorporate any number of variations, alterations, substitutions or equivalent arrangements not heretofore described, but which are commensurate with the spirit and scope of the invention.
