JP2006092842A - Fuel cell and power generating apparatus using same - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a fuel cell capable of sealing each unit cell with reliability to thereby achieve a reduction in thickness and facilitate maintenance, and also capable of providing high starting speed and high power generation efficiency by controlling the temperature of the cells, and to provide a power generating apparatus using the same. <P>SOLUTION: The fuel cell comprises: a plate-shaped solid polymer electrolyte 1; a cathode-side electrode plate 2 disposed on one side of the solid polymer electrolyte 1; an anode-side electrode plate 3 disposed on the other side of the solid polymer electrolyte 1; a cathode-side metal plate 4 disposed on the surface of the cathode-side electrode plate 2 and allowing a gas to flow to the inner surface side; and an anode-side metal plate 5 disposed on the surface of the anode-side electrode plate 3 and allowing a fuel to flow to the inner surface side. Peripheries of the metal plates 4, 5 on both sides are mechanically coupled to each other in an electrically insulated state. A surface heating element 10 is provided on the outer surface of the cathode-side metal plate 4 or the anode-side metal plate 5. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a fuel cell using a solid polymer electrolyte and a power generation device using the same, and more particularly to a polymer fuel cell capable of reducing the thickness and a power generation device using the same.

  Polymer fuel cells that use solid polymer electrolytes such as polymer electrolytes have high energy conversion efficiency, are thin, small, and lightweight, and are therefore being actively developed for household cogeneration systems and automobiles . As a conventional structure of such a fuel cell, one shown in 11 is known (for example, see Non-Patent Document 1).

  That is, as shown in FIG. 8, the anode 101 and the cathode 102 are disposed with the solid polymer electrolyte membrane 100 interposed therebetween. Further, the unit cell 105 is configured by being sandwiched by a pair of separators 104 via a gasket 103. Each separator 104 is formed with a gas flow path groove. A flow path for reducing gas (for example, hydrogen gas) is formed by contact with the anode 101, and an oxidizing gas (for example, for example, hydrogen gas) is contacted with the cathode 102. Oxygen gas) flow paths are formed. Each gas is supplied to the electrode reaction (chemical reaction at the electrode) by the action of the catalyst supported in the anode 101 or the cathode 102 while flowing through each flow path in the unit cell 105, and the generation of current and ions Conduction occurs.

  A large number of the unit cells 105 are stacked, and the unit cells 105 are electrically connected in series to constitute the fuel cell N, and the electrode 106 can be taken out from the unit cells 105 at both ends. Such a fuel cell N is attracting attention as a power source for electric vehicles and a distributed power source for home use in various applications because of its clean and high efficiency.

  On the other hand, with the recent activation of IT technology, mobile devices such as mobile phones, notebook computers, and digital cameras tend to be frequently used, but most of these power sources use lithium ion secondary batteries. However, as mobile devices become more sophisticated, power consumption has increased and clean and highly efficient fuel cells have been attracting attention as power sources.

  However, in the conventional structure as shown in FIG. 8, there is no degree of freedom in the structure. Therefore, there is a problem in that it is difficult to reduce the thickness, size and weight required for the power supply of mobile devices and to increase the degree of freedom of the shape, and the maintainability is poor. There was also. In addition, it is difficult to supply the redox gas so as not to mix with each other in the fuel cell and to seal it, and it is difficult to reduce the size and weight of the fuel cell while satisfying these conditions. Met. In other words, conventionally, cell parts are mutually coupled with fastening parts of bolts and nuts, and a certain pressure is applied to the cell parts. Therefore, it is necessary to increase the rigidity of each member in order to ensure sealing performance. Thinning, miniaturization, weight reduction, and free shape design were difficult.

On the other hand, with respect to the fuel cell as shown in FIG. 8, a fuel cell provided with a heating means for heating the cell at startup and a plate-type heat pipe for cooling the cell during steady operation so as to be stacked in a plurality of cells. Is known (for example, Patent Document 1). In such a stacked fuel cell, heat generated by the cell reaction in the cell is difficult to escape to the outside, and a cooling means is required during steady operation. Conversely, at the time of start-up, since it is generally difficult to efficiently heat a plurality of stacked cells, the start-up speed tends to be slow. In the solid polymer electrolyte type fuel cell, if the water in the electrolyte is insufficient, the ionic conduction cannot be sufficiently performed and the output is lowered. Therefore, from the viewpoint of maintaining the water, it is necessary to maintain the electrolyte at a certain temperature or lower.
Nikkei Mechanical separate volume "Fuel Cell Development Frontline" Date of issue: June 29, 2001, Publisher: Nikkei BP, Chapter 3, PEFC, 3.1 Principles and Features p46 Japanese Patent Laid-Open No. 11-214017

  Accordingly, an object of the present invention is to reliably perform sealing for each unit cell, thereby enabling a reduction in thickness, facilitating maintenance, and obtaining high startup speed and power generation efficiency by controlling the temperature of the cell. It is an object of the present invention to provide a fuel cell and a power generation apparatus using the same.

  The above object can be achieved by the present invention as described below.

  That is, the fuel cell of the present invention includes a plate-shaped solid polymer electrolyte, a cathode-side electrode plate disposed on one side of the solid polymer electrolyte, an anode-side electrode plate disposed on the other side, and the cathode A cathode-side metal plate that is disposed on the surface of the side electrode plate and allows gas to flow to the inner surface side, and an anode-side metal plate that is disposed on the surface of the anode-side electrode plate and allows fuel to flow to the inner surface side And mechanically coupled in a state where the peripheral edges of the metal plates on both sides are electrically insulated, and a surface on the outer surface side of the cathode-side metal plate or anode-side metal plate It is characterized by providing a heating element.

  According to the fuel cell of the present invention, the cathode side metal plate enables the gas to flow to the cathode side electrode plate, and the anode side metal plate enables the fuel to flow to the anode side electrode plate. An electrode reaction can be caused by the plate, and an electric current can be extracted from the metal plate. In addition, since the peripheral edges of the metal plates are mechanically coupled in an electrically insulated state, it is possible to reliably seal each unit cell without increasing the thickness while preventing short circuit between the two. it can. This facilitates maintenance, and the cell member does not require rigidity as compared with the conventional structure shown in FIG. 8, so that each unit cell can be significantly reduced in thickness. At this time, if an independent cell using a metal plate is used to reduce the thickness as in the present invention, the amount of heat released from the metal plate increases, so that cooling is not required during steady operation. In addition, since heating can be performed directly by the sheet heating element provided on the metal plate of each cell at the time of startup, the startup speed is fast and sufficient power generation efficiency can be obtained even when the outside air is at a low temperature.

  On the other hand, the power generator according to the present invention includes the fuel cell, a temperature sensor that detects the temperature of the cathode-side metal plate or the anode-side metal plate, and the operation of the planar heating element based on a signal from the temperature sensor. And a control unit for controlling.

  According to the power generation device of the present invention, since the fuel cell is provided, it is possible to reliably perform sealing for each unit cell, thereby enabling thinning, facilitating maintenance, and controlling the temperature of the cell. High start-up speed and power generation efficiency can be obtained. Moreover, since it is preferable to control the heating by the sheet heating element so that the temperature of the metal plate is 30 to 60 ° C., the temperature sensor for detecting the temperature and the operation of the sheet heating element based on the signal are controlled. By providing the control unit to control, suitable temperature control can be performed.

  In addition, it is preferable to further include a secondary battery that applies a voltage to the planar heating element at the time of start-up and performs charging with generated power during a steady operation. When starting up, since the temperature of the cell is low, the amount of power generation is small, so an auxiliary battery is required, and the use of a secondary battery that can charge the generated power during steady operation eliminates the need for external power supply. Become.

  Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is an assembled perspective view showing an example of a unit cell of the fuel cell of the present invention, and FIG. 2 is a longitudinal sectional view showing an example of a unit cell of the fuel cell of the present invention.

  As shown in FIGS. 1 to 2, the fuel cell of the present invention includes a plate-shaped solid polymer electrolyte 1, a cathode-side electrode plate 2 disposed on one side of the solid polymer electrolyte 1, and the other side. The anode side electrode plate 3 arranged, the cathode side metal plate 4 arranged on the surface of the cathode side electrode plate 2 and allowing the gas to flow to the inner surface side, and the surface of the anode side electrode plate 3 arranged on the inner surface side And an anode-side metal plate 5 that enables the fuel to flow through. In the present embodiment, an example is shown in which a fuel flow channel 9 is formed in the anode-side metal plate 5 by etching, and an opening 4 c for naturally supplying air is formed in the cathode-side metal plate 4.

  The solid polymer electrolyte 1 may be any solid polymer membrane battery as long as it is used in conventional solid polymer membrane batteries. From the viewpoint of chemical stability and conductivity, a perfluorocarbon having a sulfonic acid group which is a super strong acid. A cation exchange membrane made of a polymer is preferably used. Nafion (registered trademark) is preferably used as such a cation exchange membrane.

  In addition, for example, a porous film made of a fluororesin such as polytetrafluoroethylene impregnated with the above Nafion or other ion conductive material, a porous film made of a polyolefin resin such as polyethylene or polypropylene, or a non-woven fabric. A material carrying Nafion or another ion conductive material may be used.

  The thinner the solid polymer electrolyte 1 is, the more effective it is to make the whole thinner. However, in consideration of ion conduction function, strength, handling property, etc., 10 to 300 μm can be used, but 25 to 50 μm is preferable. .

  The electrode plates 2 and 3 can function as a gas diffusion layer, and can supply and discharge fuel gas, oxidizing gas, and water vapor, and at the same time can exhibit a current collecting function. As the electrode plates 2 and 3, the same or different ones can be used, and it is preferable to support a catalyst having an electrode catalytic action on the base material. The catalyst is preferably supported at least on the inner surfaces 2 b and 3 b in contact with the solid polymer electrolyte 1.

  As the electrode base material, for example, conductive carbon materials such as carbon paper, fibrous carbon such as carbon fiber nonwoven fabric, and aggregates of conductive polymer fibers can be used. In general, the electrode plates 2 and 3 are prepared by adding a water-repellent substance such as a fluororesin to such a conductive porous material. When the catalyst is supported, a catalyst such as platinum fine particles and fluorine It is formed by mixing a water-repellent substance such as a resin, mixing it with a solvent to form a paste or ink, and then applying this to one side of an electrode substrate that should face the solid polymer electrolyte membrane. The

  In general, the electrode plates 2 and 3 and the solid polymer electrolyte 1 are designed according to the reducing gas and the oxidizing gas supplied to the fuel cell. In the present invention, it is preferable to use air as the oxidizing gas and hydrogen gas as the reducing gas. In addition, methanol, dimethyl ether, or the like can be used instead of the reducing gas.

  For example, when hydrogen gas and air are used, the cathode-side electrode plate 2 on the side where air is naturally supplied causes a reaction between oxygen and hydrogen ions, so that water is generated. Is preferred. In particular, under the operating conditions of low operating temperature, high current density, and high gas utilization rate, the electrode porous body is likely to be clogged (flooded) due to the condensation of water vapor, particularly at the air electrode where water is generated. Therefore, in order to obtain stable characteristics of the fuel cell over a long period of time, it is effective to ensure the water repellency of the electrode so that the flooding phenomenon does not occur.

  As the catalyst, at least one metal selected from platinum, palladium, ruthenium, rhodium, silver, nickel, iron, copper, cobalt and molybdenum, or an oxide thereof can be used. A supported one can also be used.

  The thickness of the electrode plates 2 and 3 is more effective for reducing the overall thickness as the thickness is reduced, but is preferably 50 to 500 μm in view of electrode reaction, strength, handling properties, and the like.

  The electrode plates 2 and 3 and the solid polymer electrolyte 1 may be laminated and integrated in advance by adhesion, fusion, or the like, or may simply be arranged in a stacked manner. Such a laminated body can also be obtained as a thin film electrode assembly (MEA), and may be used.

  A cathode side metal plate 4 is disposed on the surface of the cathode side electrode plate 2, and an anode side metal plate 5 is disposed on the surface of the anode side electrode plate 3. In the present embodiment, the anode side metal plate 5 is provided with a fuel inlet 5c and an outlet 5d, and a flow channel 9 is provided therebetween.

  The cathode side metal plate 4 is provided with an opening 4c for supplying oxygen in the air. As long as the cathode side electrode plate 2 can be exposed, the number, shape, size, formation position, and the like of the opening 4c may be any. However, in consideration of the supply efficiency of oxygen in the air and the current collection effect from the cathode side electrode plate 2, the area of the opening 4c is preferably 10 to 50% of the area of the cathode side electrode plate 2, In particular, 20 to 40% is preferable.

  The opening 4c of the cathode side metal plate 4 may be provided with a plurality of circular holes, slits, or the like regularly or randomly, or may be provided with a metal mesh.

  As the metal plates 4 and 5, any metal can be used as long as it does not adversely affect the electrode reaction, and examples thereof include stainless steel plates, nickel, copper, and copper alloys. However, from the viewpoint of elongation, weight, elastic modulus, strength, corrosion resistance, press workability, etching workability and the like, a stainless steel plate, nickel and the like are preferable. The metal plates 4 and 5 are preferably subjected to noble metal plating such as gold plating in order to reduce contact resistance with the electrode plates 2 and 3.

  The channel groove 9 provided in the anode side metal plate 5 may have any planar shape or cross-sectional shape as long as a channel for hydrogen gas or the like can be formed by contact with the electrode plate 3. However, in consideration of the channel density, the lamination density at the time of lamination, the flexibility, etc., it is preferable to mainly form the vertical groove 9a parallel to one side of the metal plate 5 and the vertical groove 9b. In this embodiment, a plurality of (three in the illustrated example) vertical grooves 9a are connected in series to the horizontal grooves 9b to balance the flow path density and the flow path length.

  A part of the channel groove 9 (for example, the lateral groove 9 b) of the metal plate 5 may be formed on the outer surface of the electrode plate 3. As a method of forming the flow channel groove on the outer surface of the electrode plate 3, a mechanical method such as a hot press or cutting may be used. However, it is preferable to perform groove processing by laser irradiation in order to suitably perform fine processing. From the viewpoint of performing laser irradiation, the base material for the electrode plates 2 and 3 is preferably an aggregate of fibrous carbon.

  One or a plurality of inlets 5c and outlets 5d communicating with the channel groove 9 of the metal plate 5 can be formed. In addition, although the thickness of the metal plates 4 and 5 is more effective for reducing the overall thickness as the thickness is reduced, 0.1 to 1 mm is preferable in consideration of strength, elongation, weight, elastic modulus, handling property, and the like.

  Etching is preferable as a method of forming the flow channel 9 in the metal plate 5 in view of processing accuracy and ease. In the channel groove 9 by etching, a width of 0.1 to 10 mm and a depth of 0.05 to 1 mm are preferable. The cross-sectional shape of the channel groove 9 is preferably substantially square, substantially trapezoidal, substantially semicircular, V-shaped or the like.

  Etching is also preferably used for forming the opening 4 c in the metal plate 4, thinning the outer edge of the metal plates 4, 5, and forming the inlet 5 c to the metal plate 5.

  Etching can be performed using, for example, a dry film resist or the like, after forming an etching resist having a predetermined shape on the metal surface, and then using an etching solution corresponding to the type of the metal plates 4 and 5. Further, by using two or more kinds of metal laminated plates and selectively etching each metal, the cross-sectional shape of the flow channel 9 and the thickness of the thinned outer edge can be controlled with higher accuracy. it can.

  The embodiment shown in FIG. 2 is an example in which the caulking portions (outer edge portions) of the metal plates 4 and 5 are thinned by etching. In this way, the caulking portion is etched to have an appropriate thickness, whereby sealing by caulking can be performed more easily. From this viewpoint, the thickness of the crimped portion is preferably 0.05 to 0.3 mm.

  In the present invention, the peripheral edges of the metal plates 4 and 5 are mechanically coupled in an electrically insulated state. The coupling structure includes a caulking sealing structure, a fitting sealing structure, and a fastening member. Examples include a sealing structure. In the present embodiment, an example of sealing with caulking is shown. Electrical insulation can be performed by interposing the insulating material 6, the peripheral edge of the solid polymer electrolyte 1, or both.

  In the present invention, when caulking, as shown in FIG. 2, a structure in which the solid polymer electrolyte 1 is sandwiched between the outer edges of the metal plates 4 and 5 is preferable, and the solid polymer electrolyte 1 is sandwiched with the insulating material 6 interposed. More preferable is the structure. According to such a structure, inflow of gas or the like from one of the electrode plates 2 and 3 to the other can be effectively prevented. The thickness of the insulating material 6 is preferably 0.1 mm or less from the viewpoint of thinning. In addition, it is possible to further reduce the thickness by coating the insulating material (for example, the insulating material 6 can have a thickness of 1 μm).

  As the insulating material 6, a sheet-like resin, rubber, thermoplastic elastomer, ceramics, and the like can be used. However, in order to improve the sealing performance, resin, rubber, thermoplastic elastomer, and the like are preferable, and in particular, polypropylene, polyethylene, polyester, fluorine Resin and polyimide are preferable. The insulating material 6 can be integrated with the metal plates 4 and 5 in advance by sticking or coating the peripheral edges of the metal plates 4 and 5 directly or via an adhesive.

  As the caulking structure, the structure shown in FIG. 2 is preferable from the viewpoint of sealing performance, ease of manufacture, thickness, and the like. That is, the outer edge portion 5a of one metal plate 5 is made larger than the other outer edge portion 4a, and the insulating material 6 is interposed, while the outer edge portion 5a of one metal plate 5 is changed to the outer edge portion 4a of the other metal plate 4. A caulking structure that is folded back so as to sandwich pressure is preferable. In this caulking structure, it is preferable to provide a step in the outer edge portion 4a of the metal plate 4 by pressing or the like. Such a caulking structure itself is known as metal processing, and can be formed by a known caulking device.

  In the present invention, as shown in FIGS. 1 to 2, a planar heating element 10 is provided on the outer surface side of the cathode side metal plate 4 or the anode side metal plate 5. Although the sheet heating element 10 can be provided on both the metal plates 4 and 5, the cathode side metal plate 4 is formed with an opening 4c for naturally supplying air as in the present embodiment. In this case, it is preferable to provide only the anode side metal plate 5 from the viewpoint of thermal efficiency.

  The planar heating element 10 is not particularly limited as long as it can generate heat upon application of a voltage or the like. For example, a film heater or a rubber heater can be used. In this embodiment, an example using a film heater as shown in FIG. 3 is shown.

  This film heater has a structure in which a resistor 11 such as SUS is patterned on the surface of a film 12 made of a heat resistant resin such as polyimide, and the size can be freely changed depending on the pattern of the resistor 11. . The thickness of the film 12 is about 1 to 500 μm. Moreover, an output can be fluctuate | varied with the thickness and area of the resistor 11 (for example, 1-100W).

  The pattern end portion of the resistor 11 is connected to the electrodes 11a and 11b, and the lead wire 13 can be connected thereto. The resistor 11 generates heat when a DC or AC voltage is applied. Moreover, it is also possible to provide the opening 12a as needed at positions corresponding to the fuel inlet 5c and the outlet 5d. The planar heating element 10 can be bonded to the metal plate 5 with a double-sided tape or an adhesive. Further, the resistor 11 may be patterned on the surface of the anode side metal plate 5 or the like via an insulating layer.

  The planar heating element 10 can obtain a sufficient effect even by applying a voltage at the time of start-up, but the application of the voltage to the planar heating element 10 is controlled so that the temperature of the metal plate is 30 to 60 ° C. It is preferable to do this. Therefore, as shown in FIG. 4, the power generation device of the present invention includes the above fuel cell, a temperature sensor 15 that detects the temperature of the cathode side metal plate 4 or the anode side metal plate 5, and the temperature sensor 15. And a temperature control unit 16 for controlling the operation of the sheet heating element 10 based on the above signal.

  Moreover, since it is necessary to apply a sufficient voltage to the planar heating element 10 at the time of startup, a separate power source is required. For this reason, in this embodiment, as shown in FIG. 4, an example is further provided with a secondary battery 17 that applies a voltage to the planar heating element 10 at the time of startup and performs charging with generated power during steady operation.

  The temperature sensor 15 may be any sensor that can convert a temperature change into an electrical signal, and a thermistor, a thermocouple, or the like can be used. The temperature control unit 16 only needs to perform feedback control such as on / off control of voltage application to the planar heating element 10 and proportional / integral / derivative control based on a signal from the temperature sensor 15.

  In this control, when a voltage is applied to the planar heating element 10, the secondary battery 17 is used as a power source if the voltage from the unit cell UC is less than a certain value, and if the voltage is above a certain value, the unit cell is used. UC is preferably used as a power source. In order to switch the power source like this, it is only necessary to provide switch means for detecting the output voltage from the unit cell UC and switching the power supply path.

  In order to charge the secondary battery 17 with the generated power during steady operation, the output voltage from the unit cell UC is detected, and when this is above a certain value, the charging circuit for the secondary battery 17 is What is necessary is just to provide the charging / discharging control part 18 to turn on. Further, in order to prevent overcharge of the secondary battery 17, the charge / discharge control unit 18 is controlled to detect the voltage of the secondary battery 17 and turn off the charging circuit when the voltage is above a certain value. Just do it.

  In the present invention, one or a plurality of unit cells as shown in FIG. 2 can be used. The unit cell is composed of a solid polymer electrolyte 1, a pair of electrode plates 2, 3, and a pair of metal plates 4, 5. It is also possible to construct a UC and to stack a plurality of unit cells to which the sheet heating element 10 or the like is bonded, or to arrange and use them on the same surface. By doing so, it is possible to provide a high-power fuel cell without the need to apply a certain pressure to the cell parts by mutually coupling with the fastening parts of the bolts and nuts.

  In use, a fuel supply tube can be directly joined to the fuel inlet 5c and the outlet 5d of the metal plate 5, but the thickness of the fuel cell is reduced in order to reduce the thickness of the fuel cell. A tube joint having a pipe parallel to the surface of the metal plate 5 is preferably provided.

  Since the fuel cell of the present invention can be thinned and can be designed to be small, light and free, it can be suitably used particularly for mobile devices such as mobile phones and notebook PCs.

[Other Embodiments]
(1) In the above-described embodiment, an example in which the caulking structure illustrated in FIG. 2 is employed has been described. However, in the present invention, a caulking structure as illustrated in FIGS. 5A to 5B may be employed.

  The caulking structure shown in FIG. 5A is a caulking structure in which the outer edge portions 4a and 5a of both the metal plates 4 and 5 are folded back. In this example, the metal plate 5 is not provided with a step portion, but the metal plate 4 is provided with a step portion. In this unit cell, a sealing member S is interposed between each of the metal plates 4 and 5 and the solid polymer electrolyte 1 so that the gas diffused from each of the electrode plates 2 and 3 is not mixed. .

  Furthermore, the caulking structure shown in FIG. 5B is an insulating material that insulates each of the metal plates 4 and 5 by another metal plate 7 without folding the outer edge portions 4a and 5a of both the metal plates 4 and 5. It is the crimping structure clamped via 6a, 6b. In this example, the metal plate 4 and the metal plate 5 are provided with stepped portions that are gently inclined. In the caulking structure, both the metal plates 4 and 5 can be used as they are without being pressed.

  (2) In the above-described embodiment, an example in which the channel groove is formed in the anode side metal plate by etching has been shown. However, in the present invention, the flow is applied to the anode side metal plate by a mechanical method such as press working or cutting. A road groove may be formed.

  (3) In the above-described embodiment, the example in which the fuel flow channel is formed in the anode side metal plate is shown. However, in the present invention, as shown in FIGS. 3, a fuel flow channel 3a may be formed. In that case, the anode side metal plate 5 may not be provided with a channel groove.

  In this example, the channel groove 2a is also formed in the cathode side electrode plate 2 on the side having the opening 4c, but for the purpose of improving the diffusibility of air from the opening 4c of the cathode side metal plate. The channel groove 2a may also be formed in the cathode side electrode plate 2.

  (4) In the above-described embodiment, the cathode side electrode plate is exposed as it is from the opening of the cathode side metal plate. However, in the present invention, the cathode side metal plate is hydrophobic so as to cover the opening. A porous polymer porous membrane may be laminated. The polymer porous membrane may be laminated inside or outside the cathode side metal plate.

  The average pore diameter of the polymer porous membrane is preferably 0.01 to 3 μm in order to prevent water droplets from leaking while maintaining air permeability. The thickness of the polymer porous membrane is preferably 10 to 100 μm. Examples of the material for the polymer porous membrane include fluororesins such as polytetrafluoroethylene, polyolefins such as polypropylene and polyethylene, polyurethane, and silicone resins.

  (5) In the above-described embodiment, an example in which an opening for naturally supplying air to the cathode side metal plate is shown. However, as with the anode side metal plate, air or the like is obtained by etching or pressing. The oxygen-containing gas channel groove, inlet, and outlet may be formed. In that case, as with the anode side metal plate, power generation is performed while supplying air or the like from the inlet of the cathode side metal plate.

  Examples and the like specifically showing the configuration and effects of the present invention will be described below.

[Example 1]
Nickel plate (50mm x 26mm x 0.3mm thickness) with grooves (width 0.8mm, depth 0.2mm, spacing 1.6mm, number 21), peripheral thin wall (thickness 100µm), gas introduction, discharge hole Was provided by etching with a ferric chloride aqueous solution. Thereafter, the peripheral thin portion was pressed to form a stepped portion (step 150 μm) and a peripheral portion, and the entire surface was gold-plated (plating thickness 0.5 μm) to obtain an anode side metal plate.

  Similarly, a nickel plate (50 mm × 26 mm × 0.3 mm thick) with through holes (1.0 mmφ, pitch 1.5 mm, number 350), peripheral thin portions, gas introduction and discharge holes are made of ferric chloride aqueous solution. It was provided by etching. Thereafter, the peripheral thin portion was pressed to form a step portion (step 150 μm) and a peripheral portion, and the entire surface was plated with gold (plating thickness 0.5 μm) to obtain a cathode side metal plate. Then, an insulating sheet (50 mm × 26 mm × 2 mm width, thickness 80 μm) was bonded to the peripheral edge.

A thin film electrode assembly (49.3 mm × 25.3 mm) was prepared as follows. As the platinum catalyst, a 20% platinum-supported carbon catalyst (EC-20-PTC) manufactured by US Electrochem Co., Ltd. was used. The platinum catalyst, carbon black (Akzo Ketjen Black EC), and polyvinylidene fluoride (Kayner) were mixed at a ratio of 75% by weight, 15% by weight, and 10% by weight, respectively, and dimethylformamide was added by 2.5% by weight. The catalyst paste was prepared by adding to the mixture of the platinum catalyst, carbon black, and polyvinylidene fluoride in such a ratio as to give a% polyvinylidene fluoride solution, and dissolving and mixing in a mortar. Carbon paper (TGP-H-90 manufactured by Toray Industries, Inc., thickness 300 μm) is cut into 20 mm × 43 mm, and about 20 mg of the catalyst paste prepared as described above is applied with a spatula and heated at 80 ° C. Dried in the dryer. Thus, a carbon paper carrying 4 mg of the catalyst composition was produced. The amount of platinum supported is 0.6 mg / cm ² .

  Using both the platinum catalyst-supported carbon paper produced as described above and a Nafion film (DuPont Nafion 112, 25.3 mm × 49.3 mm, thickness 25 μm) as a solid polymer electrolyte (cation exchange membrane), both surfaces thereof Then, hot pressing was performed for 2 minutes at 135 ° C. and 2 MPa using a mold. The thin film electrode assembly thus obtained is sandwiched between the two metal plates described above and crimped as shown in FIG. 2 to obtain a thin micro fuel cell having an outer dimension of 50 mm × 26 mm × 1.4 mm. I was able to.

  A film heater (6 W) having a size of 10 × 30 mm is adhered to the anode side metal plate of the fuel cell with a heat-resistant adhesive sheet, and a sensor part of the temperature control device is attached to the anode side metal plate, and the temperature is 50 ° C. The on / off control was performed.

  The battery characteristics of the fuel cell at that time were evaluated. For fuel cell characteristics, a fuel cell evaluation system manufactured by Toyo Technica was used, and pure hydrogen gas was allowed to flow to the anode side at room temperature (the cathode side was open to the atmosphere). The gas flow rate was 0.2 L / min. The obtained power density is shown in FIG.

[Example 2]
In Example 1, a fuel cell was produced in the same manner as in Example 1 except that on / off control was performed so that the temperature of the anode side metal plate was 35 ° C., and evaluation was performed in the same manner. The result is shown in FIG.

[Comparative Example 1]
In Example 1, a fuel cell was produced in the same manner as in Example 1 except that the on / off control was performed so that the temperature of the anode side metal plate was 25 ° C., and evaluated in the same manner. The result is shown in FIG.

  From the results shown in FIG. 7, it was found that controlling the temperature of the metal plate at 30 to 60 ° C. is important in obtaining high output in the present invention.

Assembly perspective view showing an example of the fuel cell (unit cell) of the present invention The longitudinal cross-sectional view which shows an example of the fuel cell (unit cell) of this invention The top view which shows an example of the planar heating element used by this invention The schematic block diagram which shows an example of the electric power generating apparatus of this invention The principal part which shows the other example of the crimping structure in the fuel cell of this invention It is a longitudinal cross-sectional view which shows the other example of the fuel cell (unit cell) of this invention, (a) is an assembly perspective view, (b) is a longitudinal cross-sectional view The graph which shows the relationship between the voltage of a fuel cell and output obtained by the Example etc. of this invention Assembly perspective view showing an example of a conventional fuel cell

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Solid polymer electrolyte 2 Cathode side electrode plate 3 Anode side electrode plate 4 Cathode side metal plate 4c Opening part 5 Anode side metal plate 5c Inlet 5d Outlet 6 Insulating material 9 Channel groove 10 Planar heating element 15 Temperature sensor 16 Temperature control unit (control unit)
17 Secondary battery

Claims (3)

A plate-shaped solid polymer electrolyte, a cathode side electrode plate disposed on one side of the solid polymer electrolyte, an anode side electrode plate disposed on the other side, and an inner surface disposed on the surface of the cathode side electrode plate A fuel cell comprising: a cathode-side metal plate that allows gas to flow to the side; and an anode-side metal plate that is disposed on the surface of the anode-side electrode plate and allows fuel to flow to the inner surface side. ,
Mechanically coupled with the peripheral edges of the metal plates on both sides being electrically insulated,
A fuel cell comprising a sheet heating element on an outer surface side of the cathode side metal plate or the anode side metal plate.   2. The fuel cell according to claim 1, a temperature sensor for detecting a temperature of the cathode side metal plate or the anode side metal plate, and a control unit for controlling the operation of the planar heating element based on a signal from the temperature sensor. A power generator comprising:   The power generation device according to claim 2, further comprising a secondary battery that applies a voltage to the planar heating element at the time of startup and performs charging with generated power at the time of steady operation.

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