JP5594744B2 - Reversible fuel cell - Google Patents

Description

  The present invention relates to a fuel cell that can store electric energy supplied at the time of charging as a gas and reconvert the stored gas into electric energy for use.

Conventionally, various rechargeable secondary batteries used mainly as a power source for portable devices have been proposed. Furthermore, in recent years, a battery equipped with a rechargeable battery has been developed for vehicles such as automobiles and trains in consideration of the environment. When a secondary battery is mounted on a vehicle, regenerative power generated during braking can be stored in the mounted battery and used as a power source for the vehicle, so that the energy efficiency of the vehicle can be increased.
Thus, for example, a nickel metal hydride secondary battery is considered suitable as a secondary battery mounted on a vehicle from various conditions such as energy density, load fluctuation followability, durability, and manufacturing cost (Patent Document 1). . The nickel metal hydride secondary battery uses a hydrogen storage alloy for the negative electrode and nickel hydroxide for the positive electrode as active materials, and is charged and discharged by exchange of protons between the positive and negative electrodes. A technique using manganese hydroxide instead of nickel hydroxide for the positive electrode is disclosed (Patent Document 2).

Similarly, it has been proposed to use a fuel cell as a power source for portable devices or a power source for vehicles. A fuel cell is a power generator that converts chemical energy into electrical energy when hydrogen and oxygen react to produce H ₂ O, and has a low environmental impact. Further, since the fuel cell can use oxygen in the air, there is an advantage that electricity can be taken out anywhere as long as hydrogen serving as fuel can be supplied, and it is not necessary to be charged with electricity unlike a secondary battery.

  A normal secondary battery is charged by electric energy and can store electricity. However, since it can only be charged in a place where electricity is supplied, convenience is not sufficient. Therefore, Patent Document 3 discloses a secondary battery that can be charged with gas. Further, Patent Document 2 discloses a fuel cell having a power storage function.

JP 2001-110381 A JP 2010-15783 A JP 2010-15729 A

By the way, in the nickel metal hydride secondary battery, generally, the capacity of the negative electrode is set in advance to be larger than the capacity of the positive electrode, thereby enabling sealing. That is, at the time of overcharging in which charging is further performed from the fully charged state, oxygen gas is generated in the positive electrode by the reaction (1) below.
OH ⁻ → 1/4 O ₂ + 1/2 H ₂ O + e ⁻ (1)

The oxygen gas generated at the positive electrode reacts with hydrogen in the hydrogen storage alloy (M) of the negative electrode by the reaction (2) below to become H ₂ O, so that the increase in pressure inside the battery is suppressed and the battery is sealed. It can be.
MH + 1/4 O ₂ → M + 1/2 H ₂ O (2)
However, M shows a hydrogen storage alloy.

  The reaction in which oxygen gas and hydrogen in the hydrogen storage alloy come into contact with each other to produce water is an exothermic reaction. That is, the electrical energy supplied to the battery during overcharging is discarded as thermal energy and cannot be taken out again as electrical energy.

  In addition, the electric capacity that can be stored in the secondary battery is regulated by the amount of the negative electrode and the positive electrode active material filled as a solid in a battery case having a predetermined volume. The mass of the reducing substance and the oxidizing substance that can be stored with respect to the mass of the active material is small as a mass ratio, for example, the hydrogen that can be stored in the hydrogen storage alloy AB5 is about 1.2% by weight. For this reason, it is difficult to significantly increase the energy density of the secondary battery.

  On the other hand, in a fuel cell, since the fuel cell itself cannot store electricity, an apparatus or member for supplying hydrogen gas and oxygen gas to the electrode portion is required. In addition, since the fuel cell is inferior in the ability to follow the load fluctuation at the time of discharge, it is difficult to apply the fuel cell alone to an application with a large load fluctuation such as a vehicle. Used in combination with a power storage device. Furthermore, since the fuel cell uses a gas diffusion electrode, which is a line where gas, liquid, and solid contact at the same time, as a reaction field, there is a structural problem that the reaction area is narrow and the reaction rate is slow. In addition, there are various problems such as the need for an expensive catalyst such as platinum.

  Since the secondary battery disclosed in Patent Document 3 can be discharged like a fuel cell if gas is supplied, the electric capacity is limited to the amount of active material like a normal secondary battery. However, an apparatus or member for supplying hydrogen gas and oxygen gas to the electrode portion is required.

  The “fuel cell storage battery” disclosed in Patent Document 2 does not require an extra device or member for supplying hydrogen gas and oxygen gas to the electrode portion, but uses manganese hydroxide as the positive electrode active material. Therefore, there is a problem that trimanganese tetroxide which does not contribute to the charge / discharge reaction is generated while charging / discharging is repeated, and the life characteristics are poor.

That is, in manganese dioxide that discharge process, varies with manganese dioxide MnO ₂ → manganese oxyhydroxide MnOOH → manganese hydroxide Mn _{(OH) 2,} can not be charged with the discharge to manganese hydroxide trimanganese tetraoxide _Mn 3 _{O 4} Is generated.

  The object of the present invention is to solve the above-mentioned problems, by storing the electrical energy supplied during overcharging as chemical energy of hydrogen and oxygen, and re-converting it into electrical energy for use. Another object of the present invention is to provide a fuel cell that is excellent in energy density and load followability and excellent in life characteristics.

A reversible fuel cell according to the present invention stores a negative electrode including a hydrogen storage alloy, a positive electrode including manganese dioxide, a hollow fiber separator interposed between the negative electrode and the positive electrode, and hydrogen gas generated in the negative electrode. And a hydrogen gas storage chamber for storing oxygen gas generated at the positive electrode.
In the present invention, the oxygen gas storage chamber and the hydrogen gas storage chamber are each separately and directly without any additional member such as a booster or a communication path between the negative electrode and the positive electrode and each storage chamber. The gas generated at the electrode is stored. A reversible fuel cell refers to a fuel cell capable of storing electricity that can reversibly convert fuel and electrical energy.

  According to this configuration, when the inside of the electrode is fully charged from the fully charged state, the electrolytic solution is electrolyzed to generate hydrogen gas from the negative electrode and oxygen gas from the positive electrode. The generated hydrogen gas and oxygen gas can be directly and independently stored in the hydrogen gas storage chamber and the oxygen gas storage chamber, respectively, without contacting or reacting with each other. Therefore, hydrogen gas and oxygen gas are stored in each storage room without requiring an additional gas supply source, supply passage, pressure booster, etc., and the stored hydrogen gas and oxygen gas are converted into electrical energy when the battery is discharged. And can be reused. When the battery is discharged, a normal discharge reaction as a hydrogen-manganese battery occurs between the positive and negative electrodes, and electric energy can be taken out. That is, since electrical energy is output through the electrode reaction of the secondary battery, rapid discharge and excellent discharge followability can be obtained.

At the time of discharge, the amount of electricity reduced by the discharge in each of the negative electrode and the positive electrode is supplemented by charging with hydrogen gas and oxygen gas stored in the hydrogen gas storage chamber and the oxygen gas storage chamber, respectively. Specifically, in the negative electrode, protons are released from the charged hydrogen storage alloy (MH) as shown in the reaction formula (3) representing the discharge reaction, but as shown in the reaction formula (4), The protons released are supplemented with hydrogen gas, and the negative electrode is maintained in a charged state.
^{MH → M + H + + e} - (3)
M + 1 / 2H ₂ → MH (4)
However, in Formula (3) and (4), M shows a hydrogen storage alloy.

On the other hand, in the positive electrode, as shown in the reaction formula (5) representing the discharge reaction, the manganese oxyhydroxide reduced from the charged manganese dioxide (MnO ₂ ) is absorbed by oxygen gas as shown in the reaction formula (6). It is oxidized again and the charged state of the positive electrode is maintained.
MnO ₂ + H ⁺ + e ⁻ → MnOOH (5)
MnOOH + O ₂ → MnO ₂ + H ₂ O (6)

  After the hydrogen gas and oxygen gas in each storage room are consumed, the battery is operated and discharged as a normal hydrogen-manganese battery.

  The manganese dioxide of the positive electrode becomes manganese oxyhydroxide by discharge, but when the manganese oxyhydroxide is charged, it returns to manganese dioxide and can be discharged. On the other hand, when manganese oxyhydroxide is brought into contact with oxygen gas, it reacts with hydrogen atoms to become manganese dioxide and can be discharged.

  That is, when charged, manganese oxyhydroxide releases hydrogen atoms and can be discharged, and hydrogen atoms are stored in the negative electrode. When the battery is further charged after being fully charged, the electrolytic solution is electrolyzed, hydrogen gas is generated from the negative electrode, and oxygen gas is generated from the positive electrode. When the generated oxygen gas is stored in a container, even if hydrogen atoms are generated in manganese dioxide when discharged, the gaseous oxygen gas reacts with the hydrogen atoms and operates like a fuel cell. Of course, since it operates also as a secondary battery, high output becomes possible.

That is, in the reversible fuel cell according to the present invention, the electric energy that can be extracted to the outside is the gas energy in each storage chamber in addition to the capacity as a secondary battery regulated by the amount of each active material of the positive and negative electrodes. It is possible to store. In this case, by increasing the pressure resistance and sealing performance of each storage chamber and the battery including the storage chamber, it is possible to increase the amount of gas stored per volume, that is, to improve the volume energy density of the battery.
The above operation and effect of the battery according to the present invention are obtained by chemically charging the negative electrode and the positive electrode with hydrogen gas and oxygen gas, respectively. In this specification, “charging the negative electrode” and “charging the positive electrode” mean that the reduction reaction at the negative electrode and the oxidation reaction at the positive electrode when the battery is charged by a normal electrochemical reaction are independently performed at each positive and negative electrode. It means to wake you up.

A zinc-manganese primary battery is widely known as an aqueous battery based on manganese dioxide as a positive electrode. Zinc-manganese batteries are used exclusively as primary batteries and are not used as secondary batteries. This is because the positive electrode of a manganese battery changes in the discharge process from manganese dioxide MnO ₂ → manganese oxyhydroxide MnOOH → manganese hydroxide Mn (OH) _2. This is because manganese Mn ₃ O ₄ is formed.
For this reason, manganese dioxide was not used as a positive electrode of a secondary battery. Therefore, the inventors considered that if manganese dioxide was discharged only to manganese oxyhydroxide, no manganese trioxide was formed and charging was possible again, so that it was not deteriorated, and this was confirmed by experiments. That is,

  Even if manganese dioxide is oxidized by discharge, it returns to manganese dioxide when brought into contact with oxygen gas, so that the reaction does not proceed to manganese hydroxide and irreversible manganese trioxide does not occur. In other words, when manganese dioxide was oxidized, it was successfully used as the positive electrode by charging the positive electrode in contact with oxygen gas.

  On the other hand, although a technique using nickel hydroxide or manganese hydroxide as a positive electrode material is disclosed (for example, Patent Document 2), nickel hydroxide is effective as a secondary battery positive electrode but reacts with oxygen to be oxidized. Therefore, it does not become a positive electrode of a reversible fuel cell as in the present invention. Further, the manganese hydroxide used as the positive electrode material in Patent Document 2 functions as a catalyst for the fuel cell positive electrode reaction, and the discharged active material does not return to the original charged state with oxygen, but the discharged active material. In the reversible fuel cell of the present invention, manganese dioxide can be charged with electricity as an active material or with oxygen gas in the reversible fuel cell of the present invention. After the active material is discharged, it reacts chemically with oxygen to return to the same material as when charged, so the reaction is completely different from that of manganese hydroxide in Patent Document 2.

  As described above, the electric capacity of the secondary battery is determined by the amount of the active material contained in the electrode material. For this reason, the secondary battery cannot be increased in energy density. On the other hand, if charging is possible with oxygen as described above, the electric capacity becomes large as shown in the example of the fuel cell.

  The feature of the present invention is that manganese dioxide is used for the positive electrode, a hydrogen storage alloy is used for the negative electrode, and each electrode is charged with oxygen gas and hydrogen gas to increase the electric capacity. Is in the place where the electric power can be taken out quickly by the secondary battery reaction. That is, the chemical energy of hydrogen and oxygen can be converted into electric energy and reused, and the energy utilization efficiency, energy density, and power can be dramatically increased. Further, most of the battery cost is the material cost of the active material, and a large electric capacity is possible with a small amount of active material, so that the battery cost can be reduced.

  The inventors have confirmed through experiments that the positive electrode and the negative electrode can be charged by contacting them with oxygen gas and hydrogen gas, respectively. FIGS. 3 and 4 show the results of experiments in which half cells are formed for each of the positive electrode and the negative electrode and charged with oxygen gas and hydrogen gas.

FIG. 3 shows charging when a hydrogen storage alloy is used as a negative electrode, silver (Ag) is used as a reference electrode, a half cell is formed using an alkaline electrolyte, and the negative electrode is charged by pressurizing hydrogen gas. The change in quantity is plotted against time. The left and right vertical axes in FIG. 3 (a) are the amount of charged hydrogen (mmol / g) relative to the unit weight of the hydrogen storage alloy and the electric capacity (mAh / g) relative to the unit weight, respectively. The horizontal axis indicates elapsed time (minutes).
In this experiment, charging was started from a state in which the negative electrode was completely discharged, and curves a and b in FIG. 3A are obtained when hydrogen gas was pressurized at 0.5 MPa and 0.3 MPa, respectively. Represents the change in the amount of charge. As can be seen from FIG. 3 (a), 10 minutes after the start of charging by supplying hydrogen gas, with respect to the theoretical value of the charging amount at each pressure in both conditions of 0.5 MPa and 0.3 MPa. It was charged to almost 80%.

  In FIG. 3B, the vertical axis represents the potential of the negative electrode (V vs. Ag / AgCl), and the horizontal axis represents the discharge amount (mAh / g). This experiment shows that the negative electrode charged with hydrogen gas can be almost completely discharged in an alkaline solution.

FIG. 4 shows a case where manganese oxyhydroxide is used as a positive electrode, silver (Ag) is used as a reference electrode, a half cell is formed using an alkaline electrolyte, and charging and discharging are performed by pressurizing oxygen gas. The potential change of the positive electrode is plotted against time. The vertical axis in FIG. 4 represents the potential of the positive electrode (V
vs. (Ag / AgCl) and the horizontal axis represents the elapsed time (minutes).
(I) in FIG. 4 (a) shows the potential with respect to the reference electrode after oxygen gas is pressurized and applied to the positive electrode. In (ii), the supply of oxygen gas was stopped and 0.2C discharge was performed. It is a graph of the case. When the positive electrode is brought into contact with oxygen gas (solid line), the battery is almost fully charged after 60 minutes, and is subsequently discharged at 0.2C. On the other hand, when the oxygen gas is not contacted (dotted line), it indicates that the battery is hardly charged. As a result, a fuel cell cathode reaction (oxidation-reduction reaction) occurred due to oxygen gas, and discharge due to the secondary battery reaction was confirmed after the oxygen gas was shut off.
FIG. 4B shows a state of charging with oxygen gas in a discharge state at 0.2 C, and shows that charging with oxygen gas is possible even during discharging.

  From the experimental results shown in FIG. 3 and FIG. 4, it was confirmed that each of the positive electrode and the negative electrode can be charged independently by supplying oxygen gas and hydrogen gas, respectively.

  Manganese dioxide has not been used as a positive electrode for secondary batteries because it produces trimanganese tetraoxide that cannot be charged when discharged to manganese hydroxide. Therefore, the inventors considered that trimanganese tetroxide would not be produced and would not deteriorate unless manganese dioxide was discharged to manganese hydroxide, and confirmed this by experiment.

FIG. 5 shows the result of an experiment examining the difference in charge / discharge cycle characteristics depending on the discharge reaction depth. Graph (a) in FIG. 5 is an XRD measurement result of the electrode before the charge / discharge cycle experiment, and graph (b) is a measurement result when charge / discharge is repeated 30 times between manganese dioxide and manganese oxyhydroxide. Yes, graph (c) shows the measurement results when charging / discharging was repeated 30 times between manganese dioxide, manganese oxyhydroxide, and manganese hydroxide.
In the case of the electrode repeatedly charged and discharged in the case of the graph (b), generation of a new peak is hardly observed except for the crystal structure of the electrode before the experiment. However, in the case of the electrode repeatedly charged and discharged in the case of the graph (c), the characteristic peak derived from manganese dioxide is almost eliminated, and the peak derived from trimanganese tetraoxide appears. From this, it was found that if discharge was stopped at the stage of manganese oxyhydroxide, trimanganese tetraoxide was not generated.

As described above, according to the reversible fuel cell according to the present invention, an additional gas supply system is provided by providing a storage chamber for storing hydrogen gas and oxygen gas directly and independently from each other in the negative electrode and the positive electrode. The electric energy supplied at the time of charging can be stored as a gas and converted into electric energy for use. As a result, energy that has been discarded as heat during overcharging in conventional sealed secondary batteries can be reused as electrical energy, improving energy utilization efficiency and storing the electrical energy to be extracted as the chemical energy of the gas Energy density can be dramatically improved.
In addition, since electric energy is input and output through the electrode reaction of the secondary battery, charging is possible and tracking performance with respect to load fluctuations is greatly improved as compared with conventional fuel cells. Moreover, such a battery can be manufactured and supplied at low cost by adopting a simple structure that does not require an additional member or device for supplying gas.

  By using manganese dioxide for the positive electrode, for example, it is more durable than manganese hydroxide, and can be said to be cheaper and more energy density than nickel hydroxide. Regarding the battery life, the formation of unchargeable substances produced by reduction to trimanganese tetroxide so far was prevented by oxygen gas, and cycle durability could be ensured.

When electric power is extracted using a chemical reaction, ΔG can be extracted as electricity and TΔS can be extracted as heat if the energy that can be extracted is ΔH. ΔH is called reaction generation heat, and is negative if it is an exothermic reaction such as a combustion reaction, and is also called a calorific value. ΔH is ΔG + TΔS. ΔG is called free energy and is energy that can be taken out as work, and is called exergy as effective energy.
TΔS is the heat generated with the reaction and is represented by the product of entropy change and temperature. And ΔG / ΔH is called exergy efficiency as the ability to extract effective energy. When a nickel metal hydride battery is charged and discharged, the storage efficiency, that is, the discharge power relative to the charge power can be increased to about 90 to 99%. However, when water is electrolyzed to hydrogen and oxygen, the exergy efficiency ΔG / Since ΔH is 83%, the power storage efficiency cannot exceed 83%.

  One of the problems to be solved by the present invention is to provide an apparatus that converts the exergy rate ΔG / ΔH as close to 1 as possible and reduces the rate of heating ΔH to electrical energy as much as possible. In order to increase the power generation efficiency ΔG / ΔH, TΔS is decreased and ΔG is increased. ΔG is a value determined by temperature and pressure. By minimizing this, ΔG / ΔH can be increased.

  When hydrogen is converted into electrical energy using a fuel cell, 17% of the heat generated by hydrogen is generated as heat. In order to reduce the amount of heat generated, high-pressure hydrogen is fed into the fuel cell and power generation can suppress the generation of heat and increase the power generation efficiency. When hydrogen is produced from electric energy using a fuel cell, heat of 17% of the calorific value of hydrogen is required. At that time, if hydrogen and oxygen are generated at normal pressure, it will work against the atmosphere and cause a loss. Become. Therefore, electrolysis is performed in a sealed space, and TΔS of 17% can be reduced. FIG. 6 shows a thermodynamic calculation result, which shows that TΔS decreases as the pressure increases.

  The reversible fuel cell according to the present invention preferably has a cylindrical exterior body that houses the negative electrode, the positive electrode, the separator, the hydrogen gas storage chamber, and the oxygen gas storage chamber. As described above, in the reversible fuel cell according to the present invention, if the gas storable amount per unit volume increases, the amount of energy that can be extracted as electricity increases. In other words, the energy density of the battery can be increased by improving the pressure resistance of the battery outer package.

In the reversible fuel cell according to the present invention, it is preferable that the hydrogen gas storage chamber is formed in a gap of the hydrogen storage alloy.
If the average value of the particle size of the hydrogen storage alloy is 20 μm, the porosity is about 35%. The size of the porosity varies depending on the filling method of the hydrogen storage alloy and can be larger than 35%. Such a gap functions as a hydrogen storage chamber.

  In the reversible fuel cell according to the present invention, the separator has a bottomed cylindrical shape, and is disposed in the inner axial direction of the exterior body, and the positive electrode has a bottomed cylindrical shape, The oxygen gas storage chamber is formed inward of the positive electrode, and is filled with a particulate hydrogen storage alloy inside the exterior body and outward of the separator. Is preferred.

Reversible fuel cell according to the present invention, the positive electrode, it includes a trimanganese tetraoxide (Mn ₃ O _4), the amount of trimanganese tetraoxide during the cathode is not more than 5% by weight desirable.

In the reversible fuel cell, the amount of trimanganese tetraoxide contained in the positive electrode is 5% or less by weight. According to this arrangement, when the trimanganese tetraoxide Mn ₃ O ₄ positive electrode of manganese dioxide can not charge and discharge progresses until the manganese hydroxide occurs is as described above, irreversible trimanganese tetraoxide Mn ₃ If O ₄ does not occur, the positive electrode can be recharged with oxygen without deterioration. If the trimanganese tetraoxide Mn ₃ O ₄ is 5% or less, the degree of deterioration is small. Therefore, the amount of trimanganese tetraoxide Mn ₃ O ₄ is preferably 2% or less by weight, and more preferably less than 0.5%.

In the reversible fuel cell according to the present invention , a hydrophilic material is disposed on a surface of the negative electrode in contact with the separator, and a hydrophobic material is disposed on a surface of the negative electrode in contact with the hydrogen storage chamber. It is desirable that Furthermore, it is desirable that a hydrophilic material is disposed on the surface of the positive electrode that contacts the separator, and a hydrophobic material is disposed on the surface of the positive electrode that contacts the oxygen storage chamber .
According to this configuration, the side of the negative electrode in contact with the separator is made hydrophilic, and the ionic conductivity is ensured by preventing the passage of gas and maintaining a state of being always wet with the electrolyte. Further, the side in contact with the hydrogen gas is made hydrophobic so that the negative electrode is not wetted and is kept in good contact with the hydrogen gas. The side of the positive electrode in contact with the separator is hydrophilic, and the ionic conductivity is ensured by preventing the passage of gas and maintaining a state of being always wet with the electrolyte. Further, the side in contact with the oxygen gas is made hydrophobic so that the positive electrode is not wetted and is kept in good contact with the oxygen gas. Since the separator always contains an electrolyte so that gas does not pass therethrough, the hydrogen gas storage chamber and the oxygen gas storage chamber are independent of each other without intermingling of hydrogen gas and oxygen gas. It can be stored.

  If the characteristics of a secondary battery with a reaction surface of solid (electrode) and liquid (electrolyte) and the characteristics of a fuel cell with a reaction surface of solid (electrode), gas and liquid can be realized in one electrode, it will be even higher. Output and large energy capacity are possible. Therefore, the interface of the electrode that contacts the electrolyte is made hydrophilic, and the interface that contacts the gas is made hydrophobic. Instead of making one surface of the electrode hydrophilic and making the other surface hydrophobic, the entire electrode may be made of a material having both hydrophilicity and hydrophobicity.

  In the reversible fuel cell according to the present invention, the electrolyte is preferably held in the oxygen gas storage chamber. The reason is that water generated when discharged is generated on the surface of the positive electrode, and water is electrolyzed at the positive electrode interface during charging.

  As described above, according to the reversible fuel cell according to the present invention, the energy utilization efficiency and the energy density can be dramatically increased without the need for an additional gas supply device, and the followability to load fluctuation is greatly improved. In addition, the life characteristics can be improved.

It is sectional drawing which shows typically the structure of the fuel cell which concerns on 1st Embodiment of this invention. It is sectional drawing which shows the structure of a hollow fiber reversible fuel cell. It is a graph which shows an experimental result when charging a hydrogen storage alloy with hydrogen gas. It is a graph which shows an experimental result when a manganese dioxide electrode is charged with oxygen gas. It is a graph which shows the XRD measurement result which investigated the change of the composition of the manganese dioxide positive electrode by the difference in discharge depth. It is the graph which calculated | required the influence by the pressure of free energy by the thermodynamic calculation.

  Hereinafter, embodiments according to the present invention will be described with reference to the drawings. However, the present invention is not limited to the embodiments.

  FIG. 1 is a cross-sectional view schematically showing the structure of a battery C1 according to the first embodiment having the basic configuration of the present invention. This battery C1 is configured as a reversible fuel cell in which a reaction mechanism of a secondary battery is incorporated in a fuel cell that converts chemical energy of hydrogen and oxygen into electric energy and is used. 4 and the positive electrode 6, the negative electrode case 1 that forms the hydrogen gas storage chamber 8, and the positive electrode case 2 that forms the oxygen gas storage chamber 9 are provided as main components.

  The negative electrode 4 contains a hydrogen storage alloy such as lanthanum nickel that is generally used in nickel-hydrogen secondary batteries as a main active material. Manganese dioxide is adopted as the active material of the positive electrode 6. As the electrolytic solution 3 interposed together with the separator 5 between the negative electrode 4 and the positive electrode 6, an alkaline aqueous solution generally used in a secondary battery, for example, a KOH aqueous solution, a NaOH aqueous solution, a LiOH aqueous solution, or the like is used. it can.

  As the negative electrode 4, for example, a paste obtained by adding a solvent to a negative electrode active material, a conductive filler, and a resin, which is applied on a substrate, molded into a plate shape, and cured can be used. Similarly, as the positive electrode 6, a positive electrode active material, a conductive filler, and a resin added with a solvent to form a paste, which is applied on a substrate, molded into a plate shape, and cured can be used. .

  Conductive fillers include carbon fiber, carbon fiber nickel-plated, carbon particles, carbon particles nickel-plated, organic fibers nickel-plated, fibrous nickel, nickel particles, nickel Any of the foils can be used alone or in combination. The resin is used as a binder, and is a thermoplastic resin with a softening temperature up to 120 ° C, a resin with a curing temperature from room temperature to 120 ° C, a resin having an evaporation temperature of 120 ° C or lower and soluble in a solvent, soluble in water A resin that dissolves in a solvent, a resin that dissolves in an alcohol-soluble solvent, or the like can be used. As the substrate, a metal plate having electrical conductivity such as a nickel plate can be used. Further, a foamed nickel sheet may be used instead of the substrate.

  The side of the negative electrode 4 that is in contact with the hydrogen gas storage chamber 8 uses a large amount of hydrophobic material so that the hydrogen storage alloy does not get wet and comes into contact with the hydrogen gas. The side in contact with the separator 5 is made hydrophilic, and the ionic conductivity is ensured by preventing the passage of hydrogen gas and keeping it always wet with the electrolyte. The side of the positive electrode 6 that is in contact with the oxygen gas storage chamber 9 uses a large amount of a hydrophobic material so that manganese dioxide does not get wet and comes into contact with oxygen gas. The side in contact with the separator 5 is made hydrophilic, and the ionic conductivity is ensured by preventing the passage of gas and maintaining a state in which the separator 5 is always wet. Hydrophobic carbon, Teflon (registered trademark) or the like may be applied or sprayed on the side of each electrode 4, 6 facing the gas storage chamber 8, 9, and hydrophilic modified nylon is used for each electrode. You may apply | coat or spray on the surface which contacts the separators 4 and 6. FIG. Further, vinyl acetate having both hydrophilic and hydrophobic properties may be granulated and used as a binder.

The separator 5 uses a membrane having a pore size that allows protons (H ⁺ ) to pass therethrough but hardly allows hydrogen gas and oxygen gas to pass therethrough. Specifically, a microporous membrane was used. As a material for forming the separator 5, for example, polyolefin fibers such as polyethylene fibers and polypropylene fibers, polyphenylene sulfide fibers, polyphenylene sulfide fibers, polyfluoroethylene fibers, polyamide fibers, and the like can be used. The separator 5 holds the electrolytic solution 3. Furthermore, in this embodiment, both surfaces of the separator 5 are wetted with water (electrolytic solution 3) to form a water-sealed separator, thereby improving gas impermeability and allowing hydrogen gas and oxygen gas to pass through the separator 5. It is more reliably prevented from contacting and reacting with each other.

  The surface of the negative electrode 4 opposite to the surface facing the positive electrode 6 is hermetically covered by the box-shaped negative electrode case 1, and the inner space of the negative electrode case 1 allows the hydrogen gas generated in the negative electrode 4 to pass through the negative electrode. 4 functions as a hydrogen gas storage chamber 8 for storing without interposing additional members such as a booster or a communication passage. Similarly, the surface of the positive electrode 6 opposite to the surface facing the negative electrode 4 is covered with a box-shaped positive electrode case 2, and the inner space of the positive electrode case 2 stores oxygen gas generated at the positive electrode. It functions as the oxygen gas storage chamber 9. The hydrogen gas storage chamber 8 and the oxygen gas storage chamber 9 are configured independently, that is, the hydrogen gas storage chamber 8 and the oxygen gas storage chamber 9 do not communicate with each other. The oxygen gas storage chamber 9 is filled with about one third of the volume of the oxygen gas storage chamber 9 with the same type of electrolyte as the electrolyte 3 interposed between the positive and negative electrodes.

  If the amount of the electrolytic solution 3 filled in the oxygen gas storage chamber 9 is small, the amount of water to be electrolyzed decreases, and the amount of hydrogen gas and oxygen gas generated during overcharge decreases. On the other hand, if the amount of the electrolytic solution is large, the gas storage volume decreases. From such a viewpoint, the amount of the electrolyte solution 3 filled in the oxygen gas storage chamber 9 is preferably in the range of 20 to 50% of the volume of the oxygen gas storage chamber 9, and is in the range of 25 to 40%. It is more preferable.

  The operation of the battery C1 configured as described above will be described. When the current continues to be supplied after the battery C1 reaches the fully charged state, hydrogen gas is generated from the negative electrode 4 and oxygen gas is generated from the positive electrode 6, respectively. These hydrogen gas and oxygen gas are stored in the hydrogen gas storage chamber 8 and the oxygen gas storage chamber 9, respectively.

  When the battery C1 is discharged, the amount of electricity reduced by the discharge is charged by the hydrogen gas and oxygen gas stored in the hydrogen gas storage chamber 8 and the oxygen gas storage chamber 9, respectively.

  Next, a battery C6 according to a second embodiment of the invention will be described using the cross-sectional view shown in FIG. This battery C6 has the same basic configuration as the battery C1 of the first embodiment described with reference to FIG. 1, but adopts a cylindrical outer body 90 as shown in FIG. 2 to improve pressure resistance performance and handling performance. Thus, the energy density is increased and the handling is facilitated. Note that the negative electrode, the positive electrode, the separator, and the electrolytic solution, which are the basic elements of the battery C6 according to the present embodiment, are the same as those in the first embodiment, except for the points that are specifically described below. A structure can be adopted.

  The internal space of the outer casing 90 formed in a cylindrical shape is filled with a particulate hydrogen storage alloy that forms the electrolytic solution 93 and the negative electrode 94. A cylindrical positive electrode 96 disposed inside a hollow fiber separator 95 is accommodated in the direction of the central axis of the outer package 90. An oxygen gas storage chamber 89 is formed in a space formed inside the positive electrode 96.

The space inside the outer body 90 and the outer space of the separator 95 is filled with a hydrogen storage alloy having an average particle diameter of 20 μm. At this time, the porosity is about 35%. The size of the porosity varies depending on the filling method of the hydrogen storage alloy and can be larger than 35%. When the average particle diameter is 5 to 50 μm, the porosity is about 30 to 60%. Such a gap constitutes a hydrogen gas storage chamber 88. Here, the average particle size is JIS
This is a value expressed by using a sphere equivalent diameter by the light scattering method of Z8910.

  As a result, in the battery C <b> 6, hydrogen gas generated by electrolysis is stored in the hydrogen gas storage chamber 88, and oxygen gas is stored in the oxygen gas storage chamber 89. Further, the negative electrode 94 can be charged with hydrogen stored in the hydrogen gas storage chamber 88, and the positive electrode 96 can be charged with oxygen gas stored in the oxygen gas storage chamber 89.

  The exterior body 90 is formed of a conductive material, specifically, nickel-plated iron. The inner surface of the outer package 90 is in contact with the particulate hydrogen storage alloy forming the negative electrode directly and through the electrolytic solution 93, and the outer package 90 functions as the negative electrode terminal of the battery C6. On the other hand, an insulating member 97 is disposed on the upper surface of the exterior body 90 to insulate the exterior body 90 functioning as a negative electrode terminal from the positive electrode 96. A disc-shaped positive electrode terminal 91 is joined to the upper end surface 96 a of the positive electrode 96.

  As a granular hydrogen storage alloy, for example, a powder obtained by adding carbon as a conductive agent and ethylene vinyl acetate copolymer (EVA) as a binder to a powder of a hydrogen storage alloy as an active material is granulated. Can be used. On the other hand, as the positive electrode 96, for example, manganese dioxide powder as an active material is added and mixed with carbon as a conductive agent and ethylene vinyl acetate copolymer (EVA) as a binder, as in the case of the negative electrode 94. Can be applied to a hollow fiber and hardened. With this structure, both poles become large solid-gas / solid-liquid reaction interfaces, the internal resistance decreases, and high-speed charge / discharge is possible.

  As described above, the preferred embodiments of the present invention have been described with reference to the drawings, but various additions, modifications, or deletions can be made without departing from the spirit of the present invention. Therefore, such a thing is also included in the scope of the present invention.

The battery C6 configured as described above operates as follows. The battery C1 can be charged with current as a secondary battery until it is fully charged.
When the current continues to be supplied after the battery C6 reaches the fully charged state, hydrogen gas is generated from the negative electrode 94 and oxygen gas is generated from the positive electrode 96. These hydrogen gas and oxygen gas are in contact with each other. Without being stored in the hydrogen gas storage chamber 88 and the oxygen gas storage chamber 89, respectively. Further, the negative electrode 94 and the positive electrode 96 are charged by hydrogen gas or oxygen gas stored in the gas storage chambers 88 and 89.

When the discharge of the battery C6 is started, a normal discharge reaction as a secondary battery occurs between the negative electrode 94 and the positive electrode 96, and a current flows to the load. At this time, in each of the negative electrode 94 and the positive electrode 96, the amount of electricity reduced by the discharge is supplemented by charging with hydrogen gas and oxygen gas stored in the hydrogen gas storage chamber 88 and the oxygen gas storage chamber 89, respectively. That is, in the negative electrode 94, the protons released from the charged hydrogen storage alloy (MH) are supplemented with hydrogen gas, and the negative electrode is maintained in the charged state (see reaction formula (4)). On the other hand, in the positive electrode 96, manganese oxyhydroxide (MnOOH) discharged (reduced) from charged manganese dioxide (MnO ₂ ) is oxidized again by oxygen gas, and the charged state of the positive electrode is maintained (reaction formula) (See (6)). After the hydrogen gas and oxygen gas in the storage chambers 88 and 89 are consumed, the battery is operated as a normal secondary battery and discharged.

That is, the battery C6 according to the present embodiment stores, as a secondary battery, electric energy supplied at the time of overcharging as gas in the storage chambers 88 and 89 in addition to energy that can be stored in the electrode by normal charging. It is possible to reconvert this into electric energy and use it.
In this case, by increasing the pressure resistance and sealing performance of the storage chambers 88 and 89 and the battery C6 including the storage chambers 88, the amount of gas stored per volume is increased, and the energy density of the battery C6 is compared with that of the conventional secondary battery. As a result, it is possible to greatly improve, for example, several tens of times. In addition, since the hydrogen gas generated at the negative electrode 94 and the oxygen gas generated at the positive electrode 96 are directly stored in each of the storage chambers 88 and 89, there is no need to additionally provide a gas booster or a communication passage. The battery can be manufactured and supplied at low cost by a simple structure.

  Furthermore, as described above, when the battery C6 is discharged, electric energy is output via the electrode reaction of the secondary battery, so that the followability to the load and the power are greatly improved as compared with the conventional fuel cell. To do. As a result, for example, a vehicle, such as a vehicle, which can be applied independently and without a power storage device such as an additional secondary battery or a capacitor, can be applied independently to an application with a large load fluctuation that requires a high output instantaneously. Become.

  In addition, in the battery C6 according to the present embodiment, the positive electrode 96 is manganese dioxide, which is excellent in durability. By using the positive electrode 96 as a positive electrode active material, both the charging speed and the life characteristics can be improved.

  The feature of the present invention is that manganese dioxide is used as the active material of the positive electrode 96. Even if manganese dioxide is oxidized by discharge, it returns to manganese dioxide when brought into contact with oxygen gas, so that the reaction does not proceed to manganese hydroxide and irreversible manganese trioxide does not occur. In other words, manganese dioxide was successfully used as the positive electrode by charging it in contact with oxygen gas at the stage of oxidation of manganese dioxide.

  The laminated battery according to the present invention can be used for a system having a natural energy power generation facility without a load following function, connected to an electric power system, peak cut, power outage backup, and prevention of instantaneous drop. Moreover, as an example applied to consumer use, it can also be used for home appliances such as mobile phones, notebook computers, refrigerators, and air conditioners.

DESCRIPTION OF SYMBOLS 1 Negative electrode case 2 Positive electrode case 3 Electrolytic solution 4 Negative electrode 5 Separator 6 Positive electrode 8 Hydrogen gas storage chamber 9 Oxygen gas storage chamber 88 Hydrogen gas storage chamber 89 Oxygen gas storage chamber 90 Exterior body 91 Positive electrode terminal 93 Electrolytic solution 94 Negative electrode 95 Separator 96 Positive electrode

Claims (4)

A negative electrode containing a hydrogen storage alloy; a positive electrode formed by applying manganese dioxide to a hollow fiber; a separator made of a hollow fiber interposed between the negative electrode and the positive electrode; and an electrolytic solution, wherein the electrolytic solution is electrolyzed A hydrogen gas storage chamber for storing hydrogen gas generated in the negative electrode, and an oxygen gas storage chamber for storing oxygen gas generated in the positive electrode by electrolysis of the electrolyte. In fuel cells,
A cylindrical exterior body that houses the negative electrode, the positive electrode, the separator, the hydrogen gas storage chamber, and the oxygen gas storage chamber; and
A reversible fuel cell in which the hydrogen gas storage chamber is configured in a gap between the hydrogen storage alloys. The separator has a bottomed cylindrical shape and is disposed in the inner axial direction of the exterior body;
The positive electrode has a bottomed cylindrical shape and is formed inside the separator;
The oxygen gas storage chamber is formed inside the positive electrode;
2. The reversible fuel cell according to claim 1 , wherein the hydrogen storage alloy is filled inside the exterior body and outside the separator. 3. The reversible fuel cell according to claim 1, wherein the electrolytic solution is held in the oxygen gas storage chamber. The positive electrode contains trimanganese tetraoxide (Mn ₃ O ₄ );
The reversible fuel cell according to claim 1, wherein the amount of trimanganese tetraoxide in the positive electrode is 5% or less by weight.

Images