Patent Application
20230387379
The present invention relates to a primary battery.
As a disposable primary battery and as a rechargeable secondary battery, alkaline batteries, manganese batteries, high-performance coin-type lithium primary batteries, nickel-cadmium batteries, nickel-metal hydride batteries, and lithium ion batteries have been widely used conventionally in small devices, sensors, mobile devices, and the like. Furthermore, in recent development of Internet of Things (IoT), development has been progressing for scattered type sensors that are to be set and used at various places in the nature, such as in the soil and in forests.
Batteries generally used currently often include a rare metal such as lithium, nickel, manganese, or cobalt, and have a resource depletion problem.
An air battery having a low environmental load has also been studied (Patent Literature 1).
Patent Literature 1: WO2018/003724
The basis of the battery of Patent Literature 1 is the basis of an air battery, and the battery uses oxygen in the air as a positive electrode active material, and therefore an air intake port is essential for the battery. Therefore, the air battery has a disadvantage that an electrolytic solution volatilizes from the air intake port and is not suitable for long-term storage. Therefore, a new battery is awaited that has a low environmental load and is capable of battery reaction in a sealed system.
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a primary battery that has a low environmental load and can be stored for a long period of time.
A primary battery according to an aspect of the present invention includes a positive electrode containing iron oxyhydroxide, a negative electrode containing magnesium or aluminum, and an electrolyte disposed between the positive electrode and the negative electrode.
According to the present invention, a primary battery can be provided that has a low environmental load and can be stored for a long period of time.
Hereinafter, an embodiment of the present invention will be described with reference to the drawings.
Specifically, the positive electrode 101 is formed using iron oxyhydroxide as an active material. The negative electrode 103 is formed using magnesium or aluminum as an active material. The aqueous electrolytic solution (electrolyte) 102 is disposed so as to be in contact with the positive electrode 101 and the negative electrode 103. As described above, the primary battery of the present embodiment is characterized in that the positive electrode 101 contains an active material of iron oxyhydroxide and the negative electrode 103 contains an active material of magnesium or aluminum.
A discharge reaction in the positive electrode 101 can be expressed as follows.
2FeOOH+2H2O+2e−→2Fe(OH)2+2OH− (1)
The hydroxide ions (OH−) in the above formula are dissolved in the aqueous electrolytic solution 102 from the positive electrode 101 by electrochemical reduction, and move to a surface of the negative electrode 103 in the aqueous electrolytic solution 102.
A discharge reaction in the negative electrode 103 can be expressed as follows. Hereinafter, a reaction will be described in which, for example, magnesium (Mg) is used in the negative electrode 103.
Mg+2OH−→Mg(OH)2+2e− (2)
The hydroxide ions (OH−) in the above formula and the negative electrode 103 react to generate (precipitate) magnesium hydroxide (Mg(OH)2). A reaction in which aluminum (Al) is used in the negative electrode 103 also causes precipitation of aluminum hydroxide (Al(OH)3) similarly to the reaction in which magnesium (Mg) is used.
By these reactions of formulas (1) and (2), discharge is possible, and a total reaction can be expressed as follows.
2FeOOH+Mg+2H2O→2Fe(OH)2+Mg(OH)2 (3)
The theoretical electromotive force is about 1.7 V (at the time of using α-FeOOH as a positive electrode active material and Mg as a negative electrode active material) or about 1.6 V (at the time of using α-FeOOH as a positive electrode active material and Al as a negative electrode active material).
In the primary battery of the present embodiment, iron oxyhydroxide is used as a positive electrode active material, magnesium or aluminum is used as a negative electrode active material, and an aqueous electrolytic solution is used as an electrolyte, and thus the primary battery can be expected to be a battery including inexpensive materials and having a low environmental load.
The positive electrode 101 can contain a positive electrode active material and a conductive auxiliary agent as constituent elements. Furthermore, the positive electrode 101 preferably contains a binder to integrate the materials.
The negative electrode 103 can contain a negative electrode active material and a conductive auxiliary agent as constituent elements. Furthermore, the negative electrode 103 preferably contains a binder to integrate the materials.
Each of the above constituent elements will be described below.
The positive electrode contains at least a positive electrode active material, and can contain additives such as a conductive auxiliary agent and a binder as necessary. The positive electrode may be formed on a sheet-like current collector containing at least one selected from the group consisting of copper, iron, and carbon.
The positive electrode active material of the present embodiment contains at least iron oxyhydroxide (FeOOH). Iron oxyhydroxide has four phases of an a phase, a 3 phase, a y phase, and a 6 phase having different crystal forms, and the a phase is preferable from the viewpoints of cost and productivity.
The positive electrode active material has a particle size of preferably 0.3 μm to 10 μm, and more preferably 0.5 μm to 5 μm.
This is because as the particle size is smaller, the number of sites to be reacted increases and the output performance is improved whereas by repeating a charge/discharge cycle, the electrical contact with the positive electrode active material, the conductive auxiliary agent, and the current collector is impaired and the cycle performance deteriorates.
Iron oxyhydroxide can be produced with an existing method such as a method of oxidizing iron hydroxide (Fe(OH)2) in a pH-controlled aqueous solution, a method of heating an iron chloride (FeCl3) aqueous solution, or a method of adding hydrogen peroxide (H2O2) to an iron hydroxide (Fe(OH)2) dispersion. Commercially available iron oxyhydroxide can also be used.
In the present embodiment, the positive electrode may contain a conductive auxiliary agent. As the conductive auxiliary agent, for example, carbon can be used. Specific examples of the conductive auxiliary agent include carbon blacks such as Ketjen black and acetylene black, activated carbons, graphites, and carbon fibers. In order to sufficiently ensure a reaction site in the positive electrode, carbon having a small particle size is suitable. Specifically, carbon having a particle size of 1 μm or less is desirable. Such carbon can be obtained, for example, as a commercially available product or by a known synthesis.
The positive electrode active material may be directly coated with carbon. Examples of the coating method include physical methods such as vapor deposition, sputtering, and a method in which a planetary ball mill is used, chemical methods such as coating with an organic substance followed by heat treatment, and known methods.
The positive electrode may contain a binder. The binder is not particularly limited, and examples of the binder include polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVDF), styrene butadiene rubber, ethylene propylene diene rubber, and natural rubber. Styrene butadiene rubber, ethylene propylene diene rubber, and natural rubber, which are formed using no fluorine, are more preferable from the viewpoints of an environmental load and disposal treatment.
These binders can be used in a powder or dispersion form.
Regarding the contents of the positive electrode active material, the conductive auxiliary agent, and the binder in the positive electrode of the present embodiment, the content of the positive electrode active material is more than 0% by weight and 99% or less and preferably 70 to 95% by weight, the content of the conductive auxiliary agent is 0 to 90% by weight and preferably 1 to 30% by weight, and the content of the binder is 0 to 50% by weight and preferably 1 to 30% by weight based on the weight of the entire positive electrode.
The positive electrode can be prepared as follows. The positive electrode can be formed by mixing an iron oxyhydroxide powder as a positive electrode active material, a carbon powder, and as necessary, a dispersion such as styrene butadiene rubber, applying the mixture to a current collector, and drying the mixture.
The current collector is not particularly limited, and for example, a sheet-like or mesh-like current collector can be used in which at least one (one element) selected from the group consisting of copper, iron, titanium, nickel, and carbon is used.
In order to assemble a battery into a bipolar stack structure described below, the current collector is preferably a sheet-like current collector. The current collector is more preferably a sheet-like current collector containing at least one selected from the group consisting of copper, iron, and carbon from the viewpoints of an environmental load and disposal. As described above, the positive electrode is preferably applied to a sheet-like current collector containing at least one selected from the group consisting of copper, iron, and carbon.
In order to increase the strength of the electrode, cold pressing or hot pressing is applied to the dried electrode, and thus a more stable positive electrode can be produced.
As described above, by producing the positive electrode containing iron oxyhydroxide as a positive electrode active material, a positive electrode highly active to a charge reaction and a discharge reaction can be obtained. Furthermore, by producing the positive electrode of the primary battery having the above-described configuration, it is possible to sufficiently draw the potential of iron oxyhydroxide as a positive electrode active material.
The negative electrode contains at least a negative electrode active material, and can contain additives such as a conductive auxiliary agent and a binder as necessary. The negative electrode may be formed on a sheet-like current collector containing at least one selected from the group consisting of copper, iron, and carbon.
The negative electrode active material of the present embodiment contains at least magnesium (Mg) or aluminum (Al).
The negative electrode active material is to contain magnesium (Mg) or aluminum (Al) as a main component, and may be an alloy containing at least one component selected from the group consisting of zinc (Zn), calcium (Ca), lithium (Li), manganese (Mn), iron (Fe), tin (Sn), and carbon (C) in addition to magnesium (Mg) or aluminum (Al).
The negative electrode active material can be produced by molding a magnesium (Mg) foil or an aluminum (Al) foil into a predetermined shape.
Magnesium (Mg) or aluminum (Al) may be used in a powder form. However, if magnesium (Mg) or aluminum (Al) is used in a powder form, the number of sites to be reacted increases and the output performance is improved whereas the progress of oxidation of magnesium (Mg) or aluminum (Al) and corrosion by the electrolytic solution is accelerated. Therefore, magnesium (Mg) or aluminum (Al) is preferably used in a foil form or a bulk form.
In the case of using the negative electrode active material in a powder form, the negative electrode may contain a conductive auxiliary agent. As the conductive auxiliary agent, for example, carbon can be used. Specific examples of the conductive auxiliary agent include carbon blacks such as Ketjen black and acetylene black, activated carbons, graphites, and carbon fibers. In order to sufficiently ensure a reaction site in the negative electrode, carbon having a small particle size is suitable. Specifically, carbon having a particle size of 1 μm or less is desirable. Such carbon can be obtained, for example, as a commercially available product or by a known synthesis.
The negative electrode active material may be directly coated with carbon. Examples of the coating method include physical methods such as vapor deposition, sputtering, and a method in which a planetary ball mill is used, chemical methods such as coating with an organic substance followed by heat treatment, and known methods.
In the case of using the negative electrode active material in a powder form, the negative electrode may contain a binder. The binder is not particularly limited, and examples of the binder include polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVDF), styrene butadiene rubber, ethylene propylene diene rubber, and natural rubber. Styrene butadiene rubber, ethylene propylene diene rubber, and natural rubber, which are formed using no fluorine, are more preferable from the viewpoints of an environmental load and disposal treatment. These binders can be used in a powder or dispersion form.
Regarding the contents of the negative electrode active material, the conductive auxiliary agent, and the binder in the case of using the negative electrode active material in a powder form, the content of the negative electrode active material is more than 0% by weight and 99% or less and preferably 70 to 95% by weight, the content of the conductive auxiliary agent is 0 to 90% by weight and preferably 1 to 30% by weight, and the content of the binder is 0 to 50% by weight and preferably 1 to 30% by weight based on the weight of the entire negative electrode.
The negative electrode can be prepared as follows. The negative electrode can be formed by processing magnesium (Mg) or aluminum (Al) into a predetermined shape and attaching the resulting negative electrode active material to a current collector by welding or the like.
The current collector is not particularly limited, and for example, a sheet-like or mesh-like current collector can be used in which at least one (one element) selected from the group consisting of copper, iron, titanium, nickel, and carbon is used.
In order to assemble a battery into a bipolar stack structure described below, the current collector is preferably a sheet-like current collector. The current collector is more preferably a sheet-like current collector containing at least one selected from the group consisting of copper, iron, and carbon from the viewpoints of an environmental load and disposal. As described above, the negative electrode is preferably formed on a sheet-like current collector containing at least one selected from the group consisting of copper, iron, and carbon.
In the case of using the negative electrode active material in a powder form, the negative electrode active material can be prepared as follows. The negative electrode can be formed by mixing a magnesium (Mg) powder or an aluminum (Al) powder as a negative electrode active material, a carbon powder, and as necessary, a dispersion such as styrene butadiene rubber, applying the mixture to a current collector, and drying the mixture.
In order to increase the strength of the electrode, cold pressing or hot pressing is applied to the dried electrode, and thus a more stable negative electrode can be produced.
As described above, by producing the negative electrode containing magnesium (Mg) or aluminum (Al) as a negative electrode active material, a highly active negative electrode can be obtained. Furthermore, by producing the negative electrode of the primary battery having the above-described configuration, it is possible to sufficiently draw the potential of magnesium (Mg) or aluminum (Al) as a negative electrode active material.
The primary battery of the present embodiment contains an aqueous electrolytic solution. This aqueous electrolytic solution is an aqueous solution containing an electrolyte in which hydroxide ions (OH−) can move between the positive electrode and the negative electrode. The aqueous electrolytic solution may contain water as a main solvent and contain a solvent other than water. As the aqueous electrolytic solution, for example, an aqueous solution can be used that is obtained by dissolving at least one electrolyte selected from the group consisting of acetates, carbonates, phosphates, pyrophosphates, metaphosphates, citrates, borates, ammonium salts, formates, hydrogen carbonates, hydroxides, and chlorides in water.
In the present embodiment, the aqueous electrolytic solution is used as the electrolyte, but a solid electrolyte such as an electrolyte in a gel form or an electrolyte in a solid form may be used. That is, the electrolyte may be in any form such as a liquid form, a cream form, a gel form, or a solid form. Furthermore, the electrolyte may be aqueous or non-aqueous.
In the case of using an acidic aqueous solution or an alkaline aqueous solution as the aqueous electrolytic solution, the electrolytic solution preferably has a pH of 5.8 or more and 8.6 or less. The performance of an electrolytic solution is usually improved as the electrolytic solution is more strongly alkaline, but in the Water Pollution Control Act as a national law, the allowable limit of pH (hydrogen ion concentration) of a waste liquid discharged into a public water area other than a sea area is set to 5.8 or more and 8.6 or less. Therefore, the pH (hydrogen ion concentration) of the aqueous electrolytic solution is preferably 5.8 or more and 8.6 or less even at the sacrifice of performance from the viewpoints of an environmental load and disposal treatment.
The primary battery of the present embodiment can include, in addition to the above constituent elements, a structural member such as a separator or a battery case, and other elements required for the primary battery. As these elements, conventionally known ones can be used, but these elements preferably do not contain a harmful substance, a rare metal, a rare earth, and the like from the viewpoints of an environmental load and disposal treatment. Furthermore, these other elements are more preferably bio-derived or biodegradable materials.
As described above, the primary battery of the present embodiment includes at least a positive electrode, a negative electrode, and an aqueous electrolytic solution, and as illustrated in
For example, the primary battery is to be obtained by assembling the elements including, as described above, a positive electrode including a positive electrode active material containing iron oxyhydroxide, a conductive auxiliary agent, and a binder, a negative electrode containing magnesium (Mg) or aluminum (Al), and an aqueous electrolytic solution disposed so as to be in contact with the positive electrode and the negative electrode, in accordance with a conventional technique.
As an embodiment of the method for manufacturing a primary battery, for example, a coin-type primary battery can be manufactured.
The illustrated coin-type primary battery uses an iron oxyhydroxide powder as a positive electrode active material. Therefore, unlike an air battery using oxygen in the air as a positive electrode active material, the positive electrode case 201 of the present embodiment needs no air intake port. That is, in the present embodiment, a sealed battery can be produced. Therefore, the primary battery of the present embodiment can be stored for a long period of time without volatilization of the electrolytic solution from an air intake port.
As an embodiment of the method for manufacturing a primary battery, for example, a primary battery having a bipolar stack structure can be manufactured.
When the primary battery of the present embodiment uses an electrolytic solution having a pH of 5.8 or more and 8.6 or less, the output performance cannot be expected. Therefore, it is preferable to increase output by forming a primary battery having a stack structure.
Specifically, first, the positive electrode 101 and the negative electrode 103 are joined to both surfaces of a current collector 322 such as a copper foil respectively to form the positive electrode 101 and the negative electrode 103 on the one current collector 322. As a result, a bipolar electrode 320 is produced in which the positive electrode 101 and the negative electrode 103 are formed on the surfaces of the current collector 322 respectively.
Outermost layer current collectors 303A and 303B are to have only one surface on which an electrode is formed, and preferably have tabs 313A and 313B for extraction of electricity, respectively. The illustrated outermost layer current collector 303A has only one surface on which the positive electrode 101 is formed, and has the tab 313A. The outermost layer current collector 303B has only one surface on which the negative electrode 103 is formed, and has the tab 313B.
The tabs 313A and 313B may be processed so as to protrude from the current collectors 303A and 303B respectively, or another metal tab may be joined to each of the current collectors 303A and 303B by ultrasonic welding, spot welding, or the like.
The current collectors 322 on each of which the positive electrode 101 and the negative electrode 103 are formed are stacked so that the positive electrode 101 and the negative electrode 103 face each other, and a separator 301 is inserted between the current collectors 322 so as to be in contact with the positive electrode 101 and the negative electrode 103. The outermost layer current collectors 303A and 303B on which the positive electrode 101 and the negative electrode 103 are formed respectively are each also stacked in a manner similar to that described above so that the positive electrode 101 and the negative electrode 103 face each other, and a separator 301 is inserted so as to be in contact with the positive electrode 101 and the negative electrode 103.
After the current collectors 303A, 303B, and 322 and the separators 301 are stacked, a peripheral portion of copper foils of the current collectors is thermally pressed using a thermally fusible sheet 302 to be sealed. However, one side (part) of the peripheral portion is to be open, without being thermally pressed, in order to inject an aqueous electrolytic solution described below.
The produced stack is sandwiched between aluminum laminate films 304 or the like, and an aqueous electrolytic solution is injected into each cell (each room), then the unsealed side of the stack and a peripheral portion of the aluminum laminate films are vacuum-sealed, and thus a bipolar stack structure primary battery can be produced.
Such a primary battery is a sealed battery that needs no air intake port, unlike an air battery using oxygen in the air as a positive electrode active material. Therefore, the primary battery of the present embodiment can be stored for a long period of time without volatilization of the electrolytic solution from an air intake port.
Hereinafter, Examples of the primary battery according to the present embodiment will be described in detail. In each of Examples, a primary battery in which magnesium (Mg) was used in the negative electrode and a primary battery in which aluminum (Al) was used in the negative electrode were produced. Note that the present invention is not limited to those described in the following Examples, and can be appropriately modified and implemented without changing the gist thereof.
In Example 1, the above-described coin-type primary battery (
An iron oxyhydroxide powder (particle size: 1 μm, Kojundo Chemical Laboratory Co., Ltd.), a Ketjen black powder (EC600JD, LION SPECIALTY CHEMICALS CO., LTD.), and a polytetrafluoroethylene (PTFE) powder were sufficiently pulverized and mixed at a weight ratio of 80:10:10 using a pounding machine, and roll-formed to produce a sheet-like electrode (thickness: 0.5 mm). This sheet-like electrode was cut into a circle having a diameter of 16 mm and pressed on a copper mesh to obtain a positive electrode.
A magnesium (Mg) foil (thickness: 150 μm, The Nilaco Corporation) and an aluminum (Al) foil (thickness: 150 μm, The Nilaco Corporation) were each cut into a circle having a diameter of 16 mm to obtain negative electrodes.
A coin-type primary battery illustrated in
A cellulose-based separator (NIPPON KODOSHI CORPORATION) cut into a circle having a diameter of 18 mm was placed on a positive electrode case 201 in which the positive electrode 101 prepared with the above-described method was disposed, and a 1.0×10−4 mol/L potassium hydroxide aqueous solution (KOH) was injected as an aqueous electrolytic solution 102 into the placed separator. The negative electrode 103 was disposed on the aqueous electrolytic solution 102, the positive electrode case 201 was covered with a negative electrode case 202, a peripheral portion of the positive electrode case 201 and the negative electrode case 202 was crimped with a coin cell crimping machine, and thus a coin-type primary battery including a propylene gasket 203 was obtained.
The battery performance of the primary battery prepared with the above-described procedure was measured. In a cycle test of the battery, a current was caused to flow at a current density per effective area of the positive electrode of 1 mA/cm2 using a charge/discharge measurement system (manufactured by BioLogic Sciences Instruments), and the discharge voltage was measured until the battery voltage decreased from an open circuit voltage to 0.60 V. The discharge test of the battery was performed under a normal living environment. The discharge capacity is represented by a value (mAh/g) per unit weight of the positive electrode active material (iron oxyhydroxide).
Table 1 below shows the discharge voltage and the discharge capacity of the primary batteries in which magnesium (Mg) and aluminum (Al) are used in the negative electrode respectively. As described above, it has been found that each primary battery in Example 1 has excellent battery performance.
In Example 2, the above-described coin-type primary battery was produced with the following procedure. The positive electrode was applied to a copper sheet-like current collector and thus prepared, and the negative electrode was welded to a copper sheet-like current collector and thus prepared. As an aqueous electrolytic solution, a 1.0×10−4 mol/L potassium hydroxide aqueous solution (KOH) as an alkaline electrolytic solution (having a pH of about 9) was used. The battery was produced and evaluated in a manner similar to that in Example 1.
An iron oxyhydroxide powder (particle size: 1 μm, Kojundo Chemical Laboratory Co., Ltd.), a Ketjen black powder (EC600JD, LION SPECIALTY CHEMICALS CO., LTD.), and styrene butadiene rubber (AA Portable Power Corporation) were sufficiently mixed at a weight ratio of 80:10:10 using a kneader (THINKY CORPORATION) to produce a slurry. This slurry was applied to a copper foil (The Nilaco Corporation) and dried in a vacuum dryer at 100° C. for 12 hours. Thereafter, the dried product was pressed at 120° C., and this sheet-like electrode was cut into a circle having a diameter of 16 mm to obtain a positive electrode.
A magnesium (Mg) foil (thickness: 150 μm, The Nilaco Corporation) and an aluminum (Al) foil (thickness: 150 μm, The Nilaco Corporation) were each cut into a circle having a diameter of 16 mm, and each of the resulting circular foils was joined to a copper foil (The Nilaco Corporation) using an ultrasonic welding machine.
Table 1 shows the discharge capacity and the discharge voltage of the primary batteries in Example 2. As shown in Table 1, the discharge capacity of the battery in which magnesium (Mg) was used in the negative electrode in Example 2 was 270 mAh/g, and this value was larger than in Example 1. The battery in which aluminum (Al) was used in the negative electrode also had a larger discharge capacity in Example 2 than in Example 1.
As shown in Table 1, the discharge voltage in Example 2 is larger than the discharge voltage in Example 1. That is, a larger decrease in overvoltage was observed in Example 2 than in Example 1, and improvement in the discharge energy efficiency was achieved in Example 2.
The reason for the improvement in these characteristics is considered to be because the internal resistance of the battery was reduced by forming each of the positive electrode and the negative electrode by joining to a copper sheet-like current collector and thus a battery reaction was smoothly performed.
In Example 3, the above-described coin-type primary battery was produced with the following procedure. As the aqueous electrolytic solution, an ammonium chloride aqueous solution (NH4Cl) having a pH (hydrogen ion concentration) of 5.8 was used. The pH of is the allowable limit specified in the Water Pollution Control Act for a waste liquid that can be discharged into a public water area other than a sea area.
In a manner similar to that in Example 2, the positive electrode and the negative electrode other than the aqueous electrolytic solution were prepared and the battery was produced and evaluated.
Table 1 shows the discharge capacity and the discharge voltage of the primary batteries in Example 3. As shown in Table 1, the discharge capacity of the battery in which magnesium (Mg) was used in the negative electrode in Example 3 was 251 mAh/g, and this value was equivalent to that in Example 1. In Example 3, the battery in which aluminum (Al) was used in the negative electrode also had a discharge capacity equivalent to that in Example 1.
As shown in Table 1, the discharge voltage was also equivalent to that in Example 1, and sufficient discharge energy efficiency was achieved even when the aqueous electrolytic solution having a low environmental load and high safety was used.
The reason is considered to be because the reaction efficiency of the primary battery of the present embodiment was so high that a battery reaction was smoothly performed even when the aqueous electrolytic solution nearly neutral was used.
In Example 4, the above-described primary battery having a bipolar three-stack structure was produced with the following procedure.
The battery was evaluated in a manner similar to that in Example 3. However, the measurement in the charge and discharge test was performed until the discharge voltage decreased to 1.00 V.
A magnesium (Mg) foil (thickness: 150 μm, The Nilaco Corporation) and an aluminum (Al) foil (thickness: 150 μm, The Nilaco Corporation) were each cut into 2 cm×2 cm as the negative electrodes 103, and each of the negative electrodes 103 was joined to a copper foil (The Nilaco Corporation) using an ultrasonic welding machine.
Next, an iron oxyhydroxide powder (particle size: 1 μm, Kojundo Chemical Laboratory Co., Ltd.), a Ketjen black powder (EC600JD, LION SPECIALTY CHEMICALS CO., LTD.), and styrene butadiene rubber (AA Portable Power Corporation) were sufficiently mixed at a weight ratio of 80:10:10 using a kneader (THINKY CORPORATION) to produce a slurry as the positive electrode 101. This slurry was applied, into a size of 2 cm×2 cm, to the back surface of the above-described copper foil to which the negative electrode was joined, and dried in a vacuum dryer at 100° C. for 12 hours. Thereafter, the dried product was pressed at 120° C. to obtain a bipolar electrode 320 having surfaces on which the positive electrode 101 and the negative electrode 103 were joined respectively.
However, as for an outermost layer electrode for the positive electrode 101 and an outermost layer electrode for the negative electrode 103, the positive electrode 101 and the negative electrode 103 were joined to only one surface of the above-described copper foils (the current collectors 303A and 303B) respectively. The preparation method is similar to that described above. As the copper foils (the current collectors 303A and 303B) for the outermost layers, copper foils cut into shapes having tabs 313A and 313B were used, respectively.
A primary battery having a bipolar three-stack structure illustrated in
The two bipolar electrodes 320 prepared with the above-described method were stacked so that the positive electrode 101 and the negative electrode 103 faced each other, and a separator 301 cut out into 2.2 cm×2.2 cm and a frame-shaped thermally fusible sheet 302 having a cut-out center portion were inserted between the bipolar electrodes 320. After stacking, three sides of a peripheral portion of the current collectors 322 were thermally pressed at 180° C. to be sealed.
As for the outermost layers, in a manner similar to that described above, the negative electrode 103, the positive electrode 101, the separators 301, and the thermally fusible sheet 302 for the outermost layers were also stacked so that the positive electrode 101 and the negative electrode 103 faced each other, and the same three sides as the sides sealed above were thermally pressed to be sealed.
The stack thus produced was sandwiched between the aluminum laminate films 304 and the thermally fusible sheet 302, and the same three sides as the sides sealed above were thermally pressed to form the aluminum laminate films into a bag shape.
Thereafter, an ammonium chloride aqueous solution (NH4Cl) having a pH of 5.8 was injected into each cell (room) of the stack structure, the separators 301 were sufficiently immersed in the ammonium chloride aqueous solution, then one unsealed side of the aluminum laminate films 304 was vacuum-sealed, and finally one unsealed side of the stack was sealed from the above of the aluminum laminate films 304, and thus a bipolar stack primary battery was obtained.
In Example 4, the bipolar three-stack primary battery was produced, but a bipolar three or more-stack primary battery can be produced, and in this case, it is only required to increase the number of bipolar electrodes 320 to be stacked.
Table 1 shows the discharge capacity and the discharge voltage of the primary batteries in this Example. As shown in Table 1, the discharge capacity of the battery in which magnesium (Mg) was used in the negative electrode in Example 4 was 272 mAh/g, and this value was equivalent to that in Example 2. In Example 3, the battery in which aluminum (Al) was used in the negative electrode also had a discharge capacity equivalent to that in Example 2.
Furthermore, as shown in Table 1, the discharge voltage is also about three times that in Example 1, and thus a voltage equivalent to that of a conventional lithium ion battery can be achieved by forming a bipolar stack structure primary battery.
From the above results, the primary battery of the present embodiment has a low environmental load and can simplify disposal treatment by using iron oxyhydroxide as the positive electrode active material and using magnesium or aluminum as the negative electrode active material.
The primary battery of the present embodiment is a sealed battery that needs no air intake port unlike an air battery. Therefore, the primary battery of the present embodiment can be stored for a long period of time without volatilization of the electrolytic solution from an air intake port.
As the electrolyte, an aqueous electrolytic solution is preferably used. If an organic electrolytic solution is used, a fire, an explosion, and the like may be caused because the organic electrolytic solution easily burns, and there is a concern about an adverse effect on a human body and an environment at the time of leakage of the organic electrolytic solution. On the other hand, in the present embodiment, an aqueous electrolytic solution is used, and thus an inexpensive battery having high safety can be produced.
The aqueous electrolytic solution preferably has a pH of 5.8 or more and 8.6 or less. As a result, a battery can be produced that is environmentally friendly and can be easily discarded.
Therefore, the primary battery of the present embodiment can be effectively used as a new drive source for various electronic devices such as small devices, sensors, and mobile devices.
Note that the present invention is not limited to the above embodiment, and various modifications and combinations are possible within the technical idea of the present invention.
101 Positive electrode
102 Aqueous electrolytic solution (electrolyte)
103 Negative electrode
201 Positive electrode case
202 Negative electrode case
203 Propylene gasket
302 Thermally fusible sheet
303A, 303B Outermost layer current collector
304 Aluminum laminate film
320 Bipolar electrode
322 Current collector
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2020/043449 | 11/20/2020 | WO |
