NEGATIVE ELECTRODE FOR USE IN FLUORIDE ION SECONDARY BATTERY AND FLUORIDE ION SECONDARY BATTERY INCLUDING SAME

Abstract

Provided is a fluoride ion secondary battery having a capacity larger than that of a conventional one. A negative electrode for use in such a fluoride ion secondary battery includes a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material. The complex of Li.sub.3AlF.sub.6 and AlF.sub.3 preferably has a molar ratio of AlF.sub.3 to Li.sub.3AlF.sub.6 of 0.1 to 2. The content of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 in the negative electrode is preferably 25% by mass or less. The complex of Li.sub.3AlF.sub.6 and AlF.sub.3 is preferably in an amorphous state.

Claims

1. A negative electrode for use in a fluoride ion secondary battery, the negative electrode comprising a negative electrode active material comprising a complex of Li.sub.3AlF.sub.4 and AlF.sub.3.

2. The negative electrode according to claim 1, wherein the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 has a molar ratio of AlF.sub.3 to Li.sub.3AlF.sub.6 of 0.1 to 2.

3. The negative electrode according to claim 1, wherein the content of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 is 25% by mass or less.

4. The negative electrode according to claim 1, wherein the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 is in an amorphous state.

5. A fluoride ion secondary battery comprising the negative electrode according to claim 1.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0019] FIG. 1 is a diagram showing a method for synthesizing a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material according to an embodiment of the present invention;

[0020] FIG. 2 is a graph showing an X-ray diffraction spectrum of a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material according to the embodiment;

[0021] FIG. 3 is a view showing the properties of a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 and conventional modified AlF.sub.3;

[0022] FIG. 4 is a diagram showing an exemplary method for producing a negative electrode according to an embodiment of the present invention for use in a fluoride ion secondary battery;

[0023] FIG. 5 is a diagram showing an exemplary method for producing a conventional negative electrode for use in a fluoride ion secondary battery;

[0024] FIG. 6 is a graph showing an NMR spectrum of a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material according to the embodiment; and

[0025] FIG. 7 is a graph showing the charging and discharging curves of the negative electrode half cells of Examples 1 and 2, Reference Example 1, and Comparative Example 1 for fluoride ion secondary batteries.

DETAILED DESCRIPTION OF THE INVENTION

[0026] Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

Negative Electrode for Use in Fluoride Ion Secondary Battery

[0027] The negative electrode according to an embodiment of the present invention for use in a fluoride ion secondary battery includes a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material. A negative electrode including a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 and being for use in a fluoride ion secondary battery has not been known so far. The negative electrode according to the embodiment for use in a fluoride ion secondary battery is characterized by including a complex of Li.sub.3AlF.sub.6 and AlF.sub.3.

[0028] The complex of Li.sub.3AlF.sub.6 and AlF.sub.3 functions as a negative electrode active material during charging and discharging.

[0029] Specifically, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 releases fluoride ions F.sup.− during charging, and stores fluoride ions F.sup.− during discharging.

[0030] The complex of Li.sub.3AlF.sub.6 and AlF.sub.3 according to the embodiment may be in the form of particles in each of which Li.sub.3AlF.sub.6 and AlF.sub.3 form a complex. In the complex, Li.sub.3AlF.sub.6 has ionic conductivity and functions not only as a source of fluorine but also as a catalyst for promoting defluorination of AlF.sub.3, which would otherwise be usually difficult to defluorinate.

[0031] The complex of Li.sub.3AlF.sub.6 and AlF.sub.3 preferably has a molar ratio of AlF.sub.3 to Li.sub.3AlF.sub.6 of 0.1 to 2. Namely, Li.sub.3AlF.sub.6 and AlF.sub.3 preferably coexist in a molar ratio of 1/0.1 to 1/2 in the complex. If the molar ratio of AlF.sub.3 to Li.sub.3AlF.sub.6 is less than 0.1, the defluorination of AlF.sub.3 may fail to be effectively promoted. If the molar ratio of AlF.sub.3 to Li.sub.3AlF.sub.6 is more than 2, the content of AlF.sub.3, which has insulating properties, may be so high as to result in a reduction in ionic conductivity, which may make it impossible to provide an operable battery.

[0032] Next, a method for synthesizing the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 will be described with reference to FIG. 1. FIG. 1 is a diagram showing a method for synthesizing the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material according to an embodiment of the present invention. As shown in FIG. 1, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 according to the embodiment may be synthesized by mixing LiF and AlF.sub.3 in a given ratio and sintering the mixture. The mixture is subjected to, for example, 40 cycles of ball milling at 400 rpm for 15 minutes and then sintered, for example, at 900° C. for 3 hours. The sintered product is pulverized to give the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material according to the embodiment.

[0033] The sintering is preferably carried out at a temperature in the range of 850° C. to 900° C. Since the raw material LiF has a melting point of 850° C., LiF and AlF.sub.3 can be melted and uniformly mixed with each other in such a sintering temperature range. If the sintering temperature exceeds 900° C., the raw materials may evaporate and the sintered product weight may begin to decrease significantly, which is not desirable.

[0034] The sintering at a temperature in the range of 850° C. to 900° C. is preferably carried out for a time period in the range of 2 hours to 3 hours. If the sintering time period is less than 2 hours, LiF may insufficiently react with AlF.sub.3, which is not desirable. If the sintering time period is more than 3 hours, the raw materials may evaporate so that a low yield may occur, which is not desirable.

[0035] After the sintering, the pulverization may be, for example, crushing in an agate mortar or the like. The particles resulting from the pulverization are microparticles. The microparticles are further pulverized by ball milling in the process of preparing a negative electrode material mixture powder as described later.

[0036] In this process, LiF and AlF.sub.3 are preferably mixed in a LiF/AlF.sub.3 molar ratio in the range of 1/1 to 3/1.1. When they are mixed in a molar ratio in such a range and sintered, the resulting complex can have a molar ratio of AlF.sub.3 to Li.sub.3AlF.sub.6 of 0.1 to 2 as mentioned above. If the amount of LiF is less than 1 mole relative to 1 mole of AlF.sub.3, a large portion of AlF.sub.3, which has insulating properties, may remain unreacted, so that the ionic conductivity may decrease. If the amount of LiF is more than than 3 moles relative to 1 mole of AlF.sub.3, a large portion of LiF, which has insulating properties, may remain unreacted, so that the ionic conductivity may decrease.

[0037] If LiF and AlF.sub.3 are mixed in a LiF/AlF.sub.3 molar ratio of 3/1 and sintered, Li.sub.3AlF.sub.6 can be synthesized and the resulting Li.sub.3AlF.sub.6 can function as a negative electrode active material. In such a case, however, the use of a relatively large amount of the lithium element may raise a concern about an increase in cost. According to the embodiment, however, the amount of LiF used can be reduced, which should be preferred in terms of cost.

[0038] FIG. 2 is a graph showing an X-ray diffraction spectrum of a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material according to the embodiment. The graph of FIG. 2 shows the X-ray diffraction spectra of, from the top, synthetic products obtained according to the synthesis method shown in FIG. 1, AlF.sub.3 (theoretically calculated value), LiF (theoretically calculated value), and Li.sub.3AlF.sub.6 (theoretically calculated value). The synthetic products shown in FIG. 2 are, from the top, a product synthesized from LiF and AlF.sub.3 in a LiF/AlF.sub.3 molar ratio of 3/1, a product synthesized from LiF and AlF.sub.3 in a LiF/AlF.sub.3 molar ratio of 2/1, and a product synthesized from LiF and AlF.sub.3 in a LiF/AlF.sub.3 molar ratio of 1/1.

[0039] As shown in FIG. 2, the X-ray diffraction spectra of the products synthesized from LiF and AlF.sub.3 in molar ratios of 2/1 and 1/1 each have Li.sub.3AlF.sub.6-derived peaks and AlF.sub.3-derived peaks while the peaks derived from the raw material LiF disappear from the spectra. Meanwhile, the X-ray diffraction spectrum of the product synthesized from LiF and AlF.sub.3 in a molar ratio of 3/1 has only Li.sub.3AlF.sub.6-derived peaks while the peaks derived from the raw materials LiF and AlF.sub.3 all disappear from the spectrum. This means that the X-ray diffraction spectra of FIG. 2 demonstrate that the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 according to the embodiment can be produced when LiF and AlF.sub.3 are mixed in a LiF/AlF.sub.3 molar ratio of 1/1 to 3/1.1 in the synthesis method shown in FIG. 1.

[0040] The negative electrode active material according to the embodiment is preferably in an amorphous state. The X-ray diffraction spectra of FIG. 2 show that the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 (negative electrode active material) as synthesized by the method described above is in a crystalline state. However, the crystalline state turns into an amorphous state in the process of producing the negative electrode according to the embodiment for use in a fluoride ion secondary battery as described later. The complex of Li.sub.3AlF.sub.6 and AlF.sub.3 (negative electrode active material) as synthesized by the method described above is considered to have an unstable crystal structure, which can be destroyed and turned into an amorphous state by ball milling in the process described later. It is expected that when the negative electrode active material according to the embodiment is in an amorphous state, Li.sub.3AlF.sub.6 can be tightly bonded to a solid electrolyte or a conductive aid to form good boundaries.

[0041] The content of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 in the negative electrode according to the embodiment for use in a fluoride ion secondary battery is preferably 25% by mass or less. In this regard, when the modified AlF.sub.3 produced by doping aluminum fluoride with lithium metal is used according to the conventional art, the content of the modified AlF.sub.3 in the conventional negative electrode for use in a fluoride ion secondary battery is up to 12.5% by mass. In contrast, the content of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 according to the embodiment in the negative electrode for use in a fluoride ion secondary battery can be increased up to 25% by mass. This means that the embodiment makes it possible to provide a battery with a capacity significantly larger than that of the conventional one.

[0042] The complex of Li.sub.3AlF.sub.6 and AlF.sub.3 according to the embodiment is preferably in the form of particles with an average particle size on the order of micrometers. The conventional modified AlF.sub.3, which is a lithium metal-doped aluminum fluoride material, is in the form of particles with an average particle size on the order of nanometers. In the embodiment, however, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material can be more densified when in the form of particles with an average particle size on the order of micrometers. This makes it possible to achieve higher ionic conductivity and to provide a battery with a larger capacity. The Li.sub.3AlF.sub.6—AlF.sub.3 complex in the form of microparticles with an average particle size on the order of micrometers can be produced using AlF.sub.3 and LiF as raw materials each in the form of microparticles with an average particle size on the order of micrometers. In contrast to the conventional modified AlF.sub.3, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 according to the embodiment can be further increased in particle size by the sintering step, which is carried out later.

[0043] FIG. 3 is a view showing the properties of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 and the conventional modified AlF.sub.3 produced by doping aluminum fluoride with lithium metal. More specifically, FIG. 3 shows the measured values of the densities of: Li.sub.3AlF.sub.6—AlF.sub.3 complexes, including a product synthesized from LiF and AlF.sub.3 in a molar ratio of 2:1 and a product synthesized from LiF and AlF.sub.3 in a molar ratio of 1:1; a product synthesized from LiF and AlF.sub.3 in a molar ratio of 3:1 (namely Li.sub.3AlF.sub.6); and the conventional modified AlF.sub.3. FIG. 3 also shows their ionic conductivities at 140° C. where fluoride ion secondary batteries are assumed to be operated.

[0044] The data in FIG. 3 indicates that the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as well as Li.sub.3AlF.sub.6 can be more densified than the conventional modified AlF.sub.3 and can also have a higher ionic conductivity. Therefore, the complex of Li.sub.3AlF.sub.6 and AlF.sub.6 can be used at a higher concentration than the modified AlF.sub.3 and thus can form a battery with a larger capacity. Moreover, the increase in the volume of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 with increasing concentration can be kept relatively low, which will make it possible to increase the content of a solid electrolyte including a fluoride ion-conducting fluoride material as described later and to increase the content of a conductive aid, so that higher ionic conductivity can be achieved.

[0045] The negative electrode according to the embodiment for use in a fluoride ion secondary battery preferably further includes a fluoride ion-conducting fluoride solid electrolyte and a conductive aid in addition to the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material.

[0046] The fluoride ion-conducting fluoride may be any fluoride having fluoride ion conductivity. Examples of the fluoride ion-conducting fluoride include CeBaF.sub.x and BaLaF.sub.y, such as Ce.sub.0.95Ba.sub.0.05F.sub.2.95 and Ba.sub.0.6La.sub.0.4F.sub.2.4. When containing such a fluoride ion-conducting fluoride, the negative electrode according to the embodiment for use in a fluoride ion secondary battery can have improved fluoride ion conductivity.

[0047] The fluoride ion-conducting fluoride is preferably in the form of particles with an average particle size in the range of 0.1 μm to 100 μm. The fluoride ion-conducting fluoride in the form of particles with an average particle size in such a range can form an electrode thin layer having relatively high ionic conductivity. More preferably, the fluoride ion-conducting fluoride is in the form of particles with an average particle size in the range of 0.1 μm to 10 μm.

[0048] The conductive aid may be any type having electron conductivity. For example, the conductive aid may be carbon black or the like. The carbon black may be furnace black, Ketjen black, or acetylene black. When containing such a conductive aid, the negative electrode according to the embodiment for use in a fluoride ion secondary battery can have improved electron conductivity.

[0049] The conductive aid is preferably in the form of particles with an average particle size in the range of 20 nm to 50 nm. The conductive aid in the form of particles with an average particle size in such a range can form a lightweight electrode having high electron conductivity.

[0050] The negative electrode according to the embodiment for use in a fluoride ion secondary battery may further include additional components, such as a binder, as long as such components do not impair the advantageous effects of the embodiment.

[0051] Next, methods for producing the negative electrode according to the embodiment for use in a fluoride ion secondary battery will be described in detail with reference to FIGS. 4 and 5. FIG. 4 is a diagram showing an exemplary method for producing the negative electrode according to the embodiment for use in a fluoride ion secondary battery. FIG. 5 is a diagram showing an exemplary method for producing a conventional negative electrode for use in a fluoride ion secondary battery. Specifically, FIG. 5 shows a method for producing a negative electrode using the modified AlF.sub.3, which is a lithium metal-doped aluminum fluoride material as proposed in the conventional art.

[0052] In the exemplary production method shown in FIG. 4, first, a mixture is prepared of 700 mg of CeBaF.sub.x (Ce.sub.0.95Ba.sub.0.05F.sub.2.95), which is a fluoride ion-conducting fluoride solid electrolyte, and 50 mg of carbon black (acetylene black AB), which is a conductive aid.

[0053] Subsequently, 250 mg of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 produced by the synthesis method shown in FIG. 1 is added to the mixture, and then the resulting mixture is subjected to, for example, 40 cycles of ball milling at 300 rpm for 15 minutes. As a result, a material mixture LiAlFCB is obtained which is for the negative electrode according to the embodiment for use in a fluoride ion secondary battery. The resulting material mixture LiAlFCB and a negative electrode current collector, such as a gold foil, are then integrated by pressing at a predetermined pressure to form a negative electrode according to the embodiment for use in a fluoride ion secondary battery.

[0054] In this process, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 and the fluoride ion-conducting fluoride may be mixed in any selected ratio. As mentioned above, the content of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 in the negative electrode for use in a fluoride ion secondary battery is preferably 25% by mass or less. For an increase in charging capacity, the fluoride ion-conducting fluoride as a source of fluorine is preferably mixed in a higher ratio.

[0055] As is apparent from a comparison between FIGS. 4 and 5, the method for producing the negative electrode according to the embodiment and the method for producing the conventional negative electrode differ in the negative electrode active material added to the mixture of the fluoride ion-conducting fluoride and the conductive aid. In the method for producing the negative electrode according to the embodiment for use in a fluoride ion secondary battery, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 produced by the synthesis method described above is added as a negative electrode active material to form a mixture of the fluoride ion-conducting fluoride, the conductive aid, and the complex of Li.sub.3AlF.sub.6 and AlF.sub.3, which is a negative electrode material mixture for use in a fluoride ion secondary battery. The method and so on for producing the modified AlF.sub.3, which is a lithium metal-doped aluminum fluoride material and added in the method for producing the conventional negative electrode for use in a fluoride ion secondary battery, are described in detail in PCT/JP2019/039886.

[0056] As mentioned above, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 for use as a negative electrode active material has an unstable crystal structure, which is destroyed and turned into an amorphous state by ball milling in the process shown in FIG. 4 for producing the negative electrode according to the embodiment for use in a fluoride ion secondary battery. This means that no specific peaks can be observed in the X-ray diffraction measurement of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 used as the negative electrode active material according to the embodiment. As a solution, NMR measurement may be used in place of the X-ray diffraction measurement. The NMR measurement enables the detection of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 existing in an amorphous state as the negative electrode active material according to the embodiment.

[0057] FIG. 6 is a graph showing an NMR spectrum of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as the negative electrode active material according to the embodiment. More specifically, FIG. 6 shows a solid NMR spectrum of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 produced by the synthesis method shown in FIG. 1. The NMR measurement conditions are as shown below.

NMR Measurement Conditions

[0058] NMR system: JNM-ECA 600 manufactured by JEOL Ltd. Probe: 1.6 mm triple resonance Agilent MAS probe [0059] Temperature: room temperature [0060] Spin condition: 35 kHz [0061] Standards: LiCl for .sup.7Li, CFCl.sub.3 for .sup.19F, Al(NO.sub.3).sub.3 for .sup.27Al

[0062] FIG. 6 shows that a large peak is observed at a chemical shift of 180 ppm in the NMR spectrum of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3. The large peak is identified as a .sup.19F-derived peak characteristic of Li.sub.3AlF.sub.6. Another large peak is also observed at a chemical shift of 170 ppm. This large peak is identified as a .sup.19F-derived peak characteristic of AlF.sub.3. The results show that the solid NMR measurement enables the confirmation of the presence or absence of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 produced in an amorphous state by the method described above.

[0063] The negative electrode according to the embodiment described above for use in a fluoride ion secondary battery has advantageous effects as shown below.

[0064] The negative electrode according to the embodiment for use in a fluoride ion secondary battery includes a complex of Li.sub.3AlF.sub.6 and AlF.sub.3 as a negative electrode active material. The complex of Li.sub.3AlF.sub.6 and AlF.sub.3 can be in the form of particles in each of which Li.sub.3AlF.sub.6 and AlF.sub.3 form a complex. In the complex, Li.sub.3AlF.sub.6 has ionic conductivity and functions not only as a source of fluorine but also as a catalyst for promoting defluorination of AlF.sub.3, which would otherwise be usually difficult to defluorinate. Moreover, as mentioned above, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3, can be more densified than the conventional modified AlF.sub.3, which is a lithium metal-doped aluminum fluoride material, and can also have a higher ionic conductivity. Therefore, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 can be used at a higher concentration than the conventional modified AlF.sub.3 and thus can form a battery with a larger capacity. Furthermore, the increase in the volume of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 with increasing concentration can be kept relatively low, which will make it possible to increase the content of a fluoride ion-conducting fluoride solid electrolyte and to increase the content of a conductive aid, so that higher ionic conductivity can be achieved and that a battery with a larger capacity can be provided.

[0065] For a fluoride ion secondary battery, the negative electrode according to the embodiment can also have a high level of active material utilization for the first charge and discharge cycle and have a high coulombic efficiency. Specifically, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 according to the embodiment has an active material utilization as high as about 70′ and a coulombic efficiency as high as about 80%, whereas the conventional modified AlF.sub.3 has an active material utilization as low as about 40% and a coulombic efficiency as low as about 50%.

Fluoride Ion Secondary Battery

[0066] The fluoride ion secondary battery according to an embodiment of the present invention includes the negative electrode described above. The fluoride ion secondary battery according to the embodiment also includes a solid electrolyte layer including a fluoride ion-conducting solid electrolyte; and a positive electrode.

[0067] The solid electrolyte as a component of the solid electrolyte layer may be a conventionally known solid electrolyte. Specifically, the solid electrolyte may be a fluoride ion-conducting fluoride as described above.

[0068] The positive electrode may include a conventionally known positive electrode active material. The positive electrode preferably has a standard electrode potential sufficiently higher than that of the negative electrode according to the embodiment. A fluoride ion-free material may be selected as a positive electrode material to form a battery that can be charged at the start. In this case, the battery can be produced in a discharged state at a low energy level with improved stability of the active material in the electrode.

[0069] Examples of the positive electrode material include Pb, Cu, Sn, Bi, Ag, a conductive aid, and a binder. For example, a positive electrode material mixture including lead fluoride or tin fluoride and carbon black may be integrated with a positive electrode material for serving as a current collector, such as a lead foil, by pressing at a predetermined pressure to form a positive electrode.

[0070] Thus, the negative electrode according to the embodiment, the solid electrolyte layer, and the positive electrode may be stacked in order to form the fluoride ion secondary battery according to the embodiment. The fluoride ion secondary battery according to the embodiment can produce the same advantageous effects as shown for the negative electrode according to the embodiment described above.

[0071] The embodiments described above are not intended to limit the present invention and may be altered or modified within the scope of the invention where the objects of the present invention can be achieved. For example, while embodiments in which the present invention is applied to solid-state batteries have been described, such embodiments are not intended to limit the battery type. The present invention may also be applied to fluoride ion secondary batteries including an electrolytic solution in place of the solid electrolyte layer.

EXAMPLES

[0072] Next, examples of the present invention will be described, which are not intended to limit the scope of the present invention.

Examples 1 and 2

[0073] In each of Examples 1 and 2, a negative electrode for use in a fluoride ion secondary battery was prepared according to the method shown in FIG. 4 for producing the negative electrode according to the embodiment. A complex of Li.sub.3AlF.sub.6 and AlF.sub.3 in the form of particles with an average particle size on the order of micrometers (10 μm to 100 μm), a fluoride ion-conducting fluoride in the form of particles with an average particle size of 0.1 to 100 μm, and a conductive aid in the form of particles with an average particle size of 20 to 50 nm were used in each of Examples 1 and 2. The content of the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 in the negative electrode for use in a fluoride ion secondary battery was 25% by mass. In Example 1, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 was a product synthesized from LiF and AlF.sub.3 in a molar ratio of 1:1. In Example 2, the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 was a product synthesized from LiF and AlF.sub.3 in a molar ratio of 2:1.

Comparative Example 1

[0074] In Comparative Example 1, a negative electrode for use in a fluoride ion secondary battery was prepared using the synthesis method described in PCT/JP2019/039886 and the method shown in FIG. 5 for producing the conventional negative electrode for use in a fluoride ion secondary battery. In Comparative Example 1, modified AlF.sub.3 in the form of particles with an average particle size on the order of nanometers was used, and the content of the modified AlF.sub.3 in the negative electrode for use in a fluoride ion secondary battery was 25% by mass.

Reference Example 1

[0075] In Reference Example 1, a negative electrode for use in a fluoride ion secondary battery was prepared according to the method shown in FIG. 4 for producing the negative electrode according to the embodiment. Specifically, Li.sub.3AlF.sub.6 in the form of particles with an average particle size on the order of micrometers (10 μm to 100 μm), synthesized from LiF and AlF.sub.3 in a molar ratio of 3:1, a fluoride ion-conducting fluoride in the form of particles with an average particle size of 0.1 to 100 μm, and a conductive aid in the form of particles with an average particle size of 20 to 50 nm were used in Reference Example 1. The content of Li.sub.3AlF.sub.6 in the negative electrode for use in a fluoride ion secondary battery was 25%, by mass.

Charge and Discharge Test

[0076] The negative electrode prepared in each of the examples was used to form a half cell. The resulting half cells were subjected to a charge and discharge test at a constant current. Specifically, the constant-current charge and discharge test was carried out in a vacuum environment at 140° C. at a charging current of 0.04 mA and a discharging current of 0.02 mA with a lower limit voltage of −2.44 V and an upper limit voltage of −0.1 V using a potentio-galvanostat system (SI 12871/1255B manufactured by Solartron). The test was started from the application of the charging current.

[0077] Each half cell was prepared in the form of a cylindrical columnar pellet cell by press-molding the materials at a pressure of 40 MPa in a tablet molding machine. Specifically, a gold foil (99.99%, 10 μm in thickness, manufactured by The Nilaco Corporation) as a negative electrode current collector, 10 mg of the negative electrode material mixture powder prepared in each of the examples, 200 mg of a solid electrolyte, 30 mg of a positive electrode material mixture powder, and a lead foil (99.99%, 200 μm in thickness, manufactured by the Nilaco Corporation) serving as a positive electrode material and a positive electrode current collector were placed in order in the tablet molding machine and then press-molded to form a half cell.

Results and Discussion

[0078] FIG. 7 is a graph showing the charging and discharging curves of the negative electrode half cells of Examples 1 and 2, Reference Example 1, and Comparative Example 1 for fluoride ion secondary batteries. More specifically, FIG. 7 shows the charging and discharging curves of the half cells of Examples 1 and 2, Reference Example 1, and Comparative Example 1 at the first charge and discharge cycle. FIG. 7 indicates that the half cell of Comparative Example 1 having the negative electrode with the modified AlF.sub.3 content of 25% by mass has almost no charging or discharging capacity. In contrast, the half cells of Examples 1 and 2 having the negative electrode with the Li.sub.3AlF.sub.6—AlF.sub.3 complex content of 25% by mass were found to have charging and discharging capacities substantially the same as those of the half cell of Reference Example 1 having the negative electrode containing 25% by mass of Li.sub.3AlF.sub.6 as a negative electrode active material. The results show that the Li.sub.3AlF.sub.6—AlF.sub.3 complex content of the negative electrode according to the example for use in a fluoride ion secondary battery can be increased to 25% by mass so that a battery capacity larger than that of the conventional one can be obtained.

[0079] The actually available capacity is expressed by the active material utilization rate relative to the theoretical capacity. In this regard, while the complex of Li.sub.3AlF.sub.6 and AlF.sub.3 has a theoretical capacity of 2.48 mAh, FIG. 7 shows the result that Examples 1 and 2 provide a charging capacity of about 1.7 mAh, which shows that an active material utilization as high as about 68% can be achieved according to Examples 1 and 2. FIG. 7 also shows the result that Example 1 provides a discharging capacity of about 1.3 mAh for the charging capacity of about 1.7 mAh, which shows that a coulombic efficiency as high as about 80% can be achieved.