Abstract:
This invention provides a fuel battery comprising a solid polymer electrolyte membrane, an anode-side catalyst body and a cathode-side catalyst body disposed respectively on both sides of the solid polymer electrolyte membrane, and a fuel guide part in which the anode-side catalyst body is disposed opposite to the anode-side catalyst body on the opposite side where the anode-side catalyst body faces the solid polymer electrolyte membrane and which guides a fuel which has been externally supplied toward the center of the face of the anode-side catalyst body.

Description:
CROSS-REFERENCE TO RELATED APPLICATION 
     This application is a U.S. national stage application of International Application No. PCT/JP2006/319928, filed Oct. 5, 2006, claiming a priority date of Oct. 7, 2005, and published in a non-English language. 
     TECHNICAL FIELD 
     The present invention relates to a fuel cell having a solid polymer electrolyte membrane and an anode-side catalyst body and a cathode-side catalyst body disposed on opposite surfaces of the solid polymer electrolyte membrane. 
     BACKGROUND ART 
     A fuel cell system is known, particularly, in which a membrane electrode assembly (hereinafter, referred to as MEA) generates electricity from hydrogen induced to an anode side of a fuel cell and oxygen induced to a cathode side thereof. 
     In the past, in the fuel cell system, hydrogen was supplied to a flow path formed on a separator. 
     However, in such a flow path structure, a hydrogen density distribution is formed from the vicinity of an introduction port through which hydrogen is introduced toward the vicinity of a discharge port through which hydrogen is discharged. The density of hydrogen supplied to an anode-side catalyst body on the MEA becomes uneven, thereby causing an output voltage to fluctuate and thus lowering the output voltage. 
     In order to solve the problem, a technology has been suggested in which a plurality of protrusions are formed on a separator in order to obtain a uniform hydrogen density distribution by the pattern of the plural protrusions (see JP-A-2002-117870) 
     Herein, the above-mentioned hydrogen density distribution represents the total hydrogen mass contained in a unit volume; the same meaning is applied to the following description. 
     SUMMARY OF THE INVENTION 
     A supply mechanism for supplying hydrogen described in the above-mentioned patent document includes, similar to the conventional flow path structure, an introduction port for introducing hydrogen and a discharge port for discharging hydrogen in the vicinity of the edges of the anode-side catalyst body. In addition, the supply mechanism includes an induction path between the introduction port and the discharge port so as to enable hydrogen to be uniformly diffused over the entire surface of the anode-side catalyst body. 
     In such a supply mechanism, the introduction port and the discharge port are disposed in the vicinities of the mutually opposing edges of the anode-side catalyst body; therefore, a large distance is defined between them. For this reason, the density of hydrogen gradually lowers from the vicinity of the introduction port toward the discharge port; hence, at a portion of the anode-side catalyst body where the hydrogen density is relatively low, the output voltage is decreased lower than that of other portions. As a result, it is difficult to increase the overall output voltage of the fuel cell. 
     The present invention has been made to solve such problems, and its object is to provide a fuel cell capable of suppressing unevenness in a hydrogen density distribution, thereby increasing an output voltage. 
     To achieve the above object, in accordance with a first aspect of the present invention, there is provided a fuel cell including a solid polymer electrolyte membrane; an anode-side catalyst body and a cathode-side catalyst body disposed on opposite surfaces of the solid polymer electrolyte membrane; and a fuel inducing portion disposed on a side opposite to the side at which the anode-side catalyst body is opposed to the solid polymer electrolyte membrane so as to be opposed to the anode-side catalyst body, thereby inducing fuel supplied from the outside, toward the center of the surface of the anode-side catalyst body. 
     According to the above aspect, since the fuel is diffused in a radial shape from the center of the anode-side catalyst body, the area where the hydrogen density is uneven becomes smaller than that when the hydrogen is supplied from the introduction port provided at the edge of the anode-side catalyst body. As a result, it is possible to increase an overall output voltage of the fuel cell. 
     In accordance with a second aspect of the present invention, the fuel inducing portion includes a mechanism for decelerating the speed of fuel lower than that when the fuel was supplied from the outside. 
     In accordance with a third aspect of the present invention, the fuel cell of the present invention includes a mechanism for inducing the fuel supplied from the outside toward the anode-side catalyst body along a direction of a normal line of the surface of the anode-side catalyst body. 
     In accordance with a fourth aspect of the present invention, a fuel inducing portion as the above-described mechanism includes an anode-side member disposed apart from the anode-side catalyst body so as to be opposed to the anode-side catalyst body, and the anode-side member includes a through pore at a position corresponding to the center of the surface of the anode-side catalyst body. 
     In accordance with a fifth aspect of the present invention, a plurality of the anode-side catalyst bodies and a plurality of the through pores are provided, and the through pores are provided at positions corresponding to the centers of the respective surfaces of the anode-side catalyst bodies. 
     In accordance with a sixth aspect of the present invention, the fuel cell of the present invention includes a plurality of the anode-side catalyst bodies and a plurality of the through pores, wherein the through pores are provided at positions corresponding to the centers of the respective surfaces of the anode-side catalyst bodies, wherein the fuel inducing portion includes an introduction path through which the fuel is supplied; and induction paths connected to the introduction path and through which the fuel supplied to the introduction path is induced to the through pores, wherein the introduction path includes a terminating port connected to the induction paths, wherein the plural induction paths include a first induction path and second induction paths of which the lengths from the terminating port toward the through pores are longer than that of the first induction path, and wherein the first induction path has a cross section smaller than those of the second induction paths. 
     In accordance with a seventh aspect of the present invention, the fuel cell of the present invention includes a plurality of the anode-side catalyst bodies and a plurality of the through pores, wherein the through pores are provided at positions corresponding to the centers of the respective surfaces of the anode-side catalyst bodies, wherein the fuel inducing portion includes: an introduction path through which the fuel is supplied; and an induction path connected to the introduction path and through which the fuel supplied to the introduction path is induced to the through pores, wherein the introduction path includes a terminating port connected to the induction path, wherein the plural through pores include a first through pore and second through pores that are disposed at positions at which the distances to the terminating port are longer than that of the first through pore, and wherein the first through pore has an area smaller than those of the second through pores. 
     In accordance with an eighth aspect of the present invention, there is provided a fuel cell including a solid polymer electrolyte membrane; an anode-side catalyst body and a cathode-side catalyst body disposed on opposite surfaces of the solid polymer electrolyte membrane; and a fuel inducing portion disposed on a side opposite to the side at which the anode-side catalyst body is opposed to the solid polymer electrolyte membrane so as to be opposed to the anode-side catalyst body, thereby inducing fuel supplied from the outside toward plural locations of the surface of the anode-side catalyst body. 
     According to the above aspect, since a plurality of through pores is provided, an overall opening area can be increased larger than that when only one through pore is provided. With this arrangement, the flow rate of the fuel discharged from the through pores can be decelerated to be lower than that when only one through pore is provided. Therefore, the fuel can be sprayed at substantially uniform pressure with respect to the anode-side catalyst body. Accordingly, it is possible to make the fuel density distribution on the anode-side catalyst body more uniform. 
     In accordance with a ninth aspect of the present invention, the fuel inducing portion includes a mechanism for decelerating the speed of fuel lower than that when the fuel was supplied from the outside. 
     In accordance with a tenth aspect of the present invention, the fuel cell of the present invention includes a mechanism for inducing the fuel supplied from the outside along a direction of a normal line of the surface of the anode-side catalyst body. 
     In accordance with an eleventh aspect of the present invention, the fuel inducing portion as the above-described mechanism includes an anode-side member disposed apart from the anode-side catalyst body so as to be opposed to the anode-side catalyst body, and the anode-side member includes through pores at positions corresponding to the plural locations of the surface of the anode-side catalyst body. 
     In accordance with a twelfth aspect of the present invention, the fuel cell of the present invention includes three or more through pores, wherein the anode-side member includes a polygonal surface formed by the lines passing through the three or more through pores, and wherein in a front view of the anode-side member, the polygonal surface is disposed as a position overlapping the center of gravity the surface of the anode-side catalyst body. 
     In accordance with a thirteenth aspect of the present invention, there is provided a fuel cell system including the fuel cell according to any one of the above-described aspects, and a fuel supply portion supplying the fuel to the fuel inducing portion of the fuel cell. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  is a diagram showing the structure of a fuel cell system according to the present invention. 
         FIG. 2  is a diagram showing an example of an exploded perspective view of a fuel cell according to a first embodiment. 
         FIG. 3  is a perspective view showing the structure of an anode-side member of the fuel cell according to the first embodiment. 
         FIG. 4  is a perspective view showing the structure of a fuel introducing member of the fuel cell according to the first embodiment. 
         FIG. 5  is a diagram showing the flow of hydrogen in the F 5 -F 5  cross section of  FIG. 2 . 
         FIG. 6  is a diagram showing the flow of hydrogen in the fuel cell according to the present invention. 
         FIG. 7  is a diagram showing an example of an exploded perspective view of a fuel cell according to a first modified example of the first embodiment. 
         FIG. 8  is a perspective view showing the structure of an anode-side member of the fuel cell according to the first modified example of the first embodiment. 
         FIG. 9  is a perspective view showing the structure of a fuel introducing member of the fuel cell according to the first modified example of the first embodiment. 
         FIG. 10  is a front view showing the structure of the fuel introducing member shown in  FIG. 9 . 
         FIG. 11  is a cross sectional view showing the A-A cross section of  FIG. 10 . 
         FIG. 12  is a graph showing a hydrogen flow rate of hydrogen flowing out from respective through pores of the anode-side member of the fuel cell according to the first modified example of the first embodiment. 
         FIG. 13  is a perspective view showing the structure of an anode-side member of a fuel cell according to a second modified example of the first embodiment. 
         FIG. 14  a graph showing a hydrogen flow rate of hydrogen flowing out from respective through pores of the anode-side member of the fuel cell according to the second modified example of the first embodiment. 
         FIG. 15  is a perspective view showing the structure of an anode-side member of a fuel cell according to a second embodiment. 
         FIG. 16  is a perspective view showing the structure of an anode-side member of a fuel cell according to a first modified example of the second embodiment. 
         FIG. 17  is a perspective view showing the structure of an anode-side member of a fuel cell according to a second modified example of the second embodiment. 
         FIG. 18  is a perspective view showing the structure of a fuel cell according to a third embodiment. 
     
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     Now, embodiments of a fuel cell according to the present invention will be described in detail with reference to the drawings. In the drawings, the same or similar elements are denoted by the same reference numerals even though they are depicted in different drawings. 
     Embodiment 1 
       FIG. 1  shows the structure of a fuel cell system according to the present invention. 
     In  FIG. 1 , a fuel cell system  1  includes a fuel supply portion  100 , a fuel cell  200 , and a control circuit  300 . 
     The fuel supply portion  100  may have any structure that can generate hydrogen, and may have a structure in which hydrogen generating substance and hydrogen generation accelerating substance are mixed with each other to discharge hydrogen. Preferably, the fuel supply portion  100  may have a structure in which sodium borohydride as hydrogen generating substance and a malic acid solution as hydrogen generation accelerating substance are mixed with each other to discharge hydrogen. 
     As a combination of the hydrogen generating substance and the hydrogen generation-accelerating substance, besides the above-mentioned example, the hydrogen generating substance may be any metal hydrides that can be hydrolyzed and the hydrogen generation accelerating substance may be any hydrogen generation catalysts such as an organic acid, an inorganic acid, or ruthenium. 
     In addition, the hydrogen generating substance may be a solution of sodium borohydride and the hydrogen generation accelerating substance may be malic acid powder. As such, the combination of the hydrogen generating substance and the hydrogen generation accelerating substance can be appropriately selected as long as the mixture thereof can generate hydrogen. 
     In addition, the reaction used in the hydrogen generating portion may use any combination of metal and a basic or acid solution. 
     Furthermore, in the hydrogen generating portion, any structure that can generate hydrogen from hydrolysis may be used including a methanol reforming type wherein hydrogen is obtained from alcohols, ethers, or ketones by stem reforming and a hydrocarbon reforming type wherein hydrogen is obtained from hydrocarbons such as gasoline, kerosene, or natural gas by stem reforming. 
     As a modified example of the hydrogen generating portion, a structure using hydrogen absorbing alloys or a hydrogen storage tank may be used. 
     The control circuit  300  is connected to the fuel cell  200 . The control circuit  300  is driven by a voltage supplied from the fuel cell  200 . 
       FIG. 2  is an exploded perspective view showing an example of the fuel cell  200 . As shown in  FIG. 2 , the fuel cell  200  includes an MEA  210 , a fuel inducing portion  220 , a cathode-side pressing member  230 , and an anode-aide pressing member  240 . The fuel cell  200  also includes a gas diffusion member (not shown) and a current collector (not shown), disposed on the anode side and the cathode side of the MEA  210 , respectively. 
     The MEA  210  includes a solid polymer electrolyte membrane  211  and a cathode-side catalyst body  212  and an anode-side catalyst body (not shown) disposed on opposite surfaces of the solid polymer electrolyte membrane  211 . The anode-side catalyst body has substantially the same shape and size as the cathode-side catalyst body  212 . 
     In  FIG. 2 , the MEA  210  has an outside dimension of 80×63×0.03 mm, and the cathode- and anode-side catalyst bodies have a size of 70×53×0.03 mm. 
     The fuel inducing portion  220  is disposed on a side opposite to the side at which the anode-side catalyst body is opposed to the solid polymer electrolyte membrane  211  and induces fuel supplied from the outside toward the center of the surface of the anode-side catalyst body. In addition, the fuel inducing portion  220  may have a function of decelerating the speed of hydrogen lower than that when the hydrogen was supplied from the outside. 
     In this embodiment, the fuel inducing portion  220  is disposed on the MEA  210  close to the anode-side catalyst body substantially in parallel to the anode-side catalyst body. The fuel inducing portion  220  includes an anode-side member  221  disposed apart from the anode-side catalyst body so as to be opposed to the anode-side catalyst body. The fuel inducing portion  220  also includes a fuel introducing member  222  that is disposed on a side opposite to the side at which the anode-side member  221  is opposed to the anode-side catalyst body and that temporarily stores therein fuel introduced thereto by using the anode-side member  221 . 
     The cathode-side pressing member  230  and the anode-side pressing member  240  are all provided with a penetration portion for inducing fuel toward the MEA  210  and sandwich the MEA  210 , the gas diffusion member (not shown), and the current collector (not shown) between them. 
     In  FIG. 2 , by way of example, lattice-shaped penetration portions are formed in the cathode-side pressing member  230  and the anode-side pressing member  240 . It is to be noted that the penetration portion is not limited to such a lattice shape and any shape that can pass fuel through it can be used. 
     In addition, the cathode-side pressing member  230  and the anode-side pressing member  240  may have different shapes. Moreover, the materials of the cathode-side pressing member  230  and the anode-side pressing member  240  may be an insulating material such as a plastic or a ceramic and an electrically conductive material such as metal. 
     Further, the current collector may not be provided in the fuel cell  200 ; in such a case, the cathode-side pressing member  230  and the anode-side pressing member  240  are made of a material having electrically conductive properties. 
       FIG. 3  is a perspective view showing the structure of the anode-side member  221  of the fuel cell  200  shown in  FIG. 2 . The anode-side member  221  includes a recess portion  221 - 1  provided on a plate-shaped member close to the anode-side catalyst body, a through pore (through hole)  221 - 2 , and a first discharge port  221 - 3 . 
     The recess portion  221 - 1  is formed to a predetermined depth from a front surface when the anode-side member  221  is viewed from the front surface, i.e., from the anode-side catalyst body side. 
     The bottom surface of the recess portion  221 - 1  is preferably in parallel to the surface of the anode-side catalyst body; however, the invention is not particularly limited to this and, for example, the bottom surface may be inclined with respect to the surface of the anode-side catalyst body. Moreover, the size of the bottom surface of the recess portion is preferably greater than that of the anode-side catalyst body. 
     The through pore  221 - 2  is preferably circular shaped. In this embodiment, the through pore  221 - 2  is located on a normal line of the anode-side catalyst body surface drawn from the center (the center of gravity) of the anode-side catalyst body. 
     In addition, the through pore  221 - 2  may have other shapes than the above-mentioned circular shape; even in such cases, the center of the through pore  221 - 2  is located on the normal line described above. 
     The anode-side member  221  shown in  FIG. 3  has an outside dimension of 80×70×1.5 mm, and the recess portion  221 - 1  has a depth of 0.5 mm from the front surface in a front view of the anode-side member  221  and has a dimension of 70×53 mm. 
     Further, the through pore  221 - 2  has a diameter φ of 10 mm. 
     The first discharge port  221 - 3  is provided to discharge water flowing into the anode-side catalyst body from the cathode-side catalyst body during electricity generation to the outside. In addition, it is to be noted that absence of the first discharge port  221 - 3  does not limit the functions described in the present invention. 
       FIG. 4  is a diagram showing the structure of the fuel introducing member  222  of the fuel cell  200  shown in  FIG. 2 . The fuel introducing member  222  includes an introduction path  222 - 1 , an induction path  222 - 2 , and a second discharge port  222 - 3 . 
     The introduction path  222 - 1  includes an introduction port  222 - 1   a , which is a connecting portion to an external fuel supply portion  100  for introducing hydrogen from the outside, and a terminating port  222 - 1   b , which is an end portion of the introduction path close to the induction path  222 - 2  described after. 
     The introduction port  222 - 1   a  may be provided so as to penetrate the fuel introducing member  222  from the rear surface to the front surface in the front view thereof as shown in  FIG. 4  and may be provided on the lateral surface thereof. Alternatively, the introduction port  222 - 1   a  may be provided within the area of the induction path  222 - 2  described after. 
     When the introduction port  222 - 1   a  is provided outside the area of the induction path  222 - 2 , the terminating port  222 - 1   b  of the introduction path  222 - 1  is provided on the lateral surface in the front view of the induction path  222 - 2 . 
     In  FIG. 4 , the terminating port  222 - 1   b  is provided at the center of the upper surface in the front view of the induction path  222 - 2 ; however, the position of the terminating port  222 - 1   b  is not particularly limited to this position, but the terminating port  222 - 1   b  may be provided at any position on the lateral surface of the induction path  222 - 2 . 
     The induction path  222 - 2  is connected to the introduction path  222 - 1  and induces hydrogen supplied to the introduction path  222 - 1  toward the through pore  221 - 2 . In this embodiment, the induction path  222 - 2  includes a recess portion formed into a plate shape and provided on the anode-side catalyst body side. 
     Specifically, the hydrogen is temporarily stored in a space formed between the recess portion and a surface of the anode-side member  221  opposite to the anode-side catalyst body, and then the hydrogen is induced to the through pore  221 - 2  formed in the anode-side member  221 . 
     Since the introduced hydrogen is temporarily stored in the induction path  222 - 1 , the flow rate of the hydrogen discharged via the induction path  222 - 1  through the through pore  221 - 2  is decelerated to be lower than the flow rate of the hydrogen when it was introduced. With this arrangement, the hydrogen discharged through the through pore  221 - 2  is diffused at substantially uniform pressure with respect to the anode-side catalyst body. For this reason, it is possible to make the hydrogen density distribution on the anode-side catalyst body more uniform and thus to increase an overall output voltage of the fuel cell. 
     In addition, the induction path  222 - 2  only needs to have a flow path for inducing hydrogen toward the through pore  221 - 2  and does not necessarily have the recess portion. The induction path  222 - 2  may, for example, have a tube shape or a pipe shape that connects the terminating port  222 - 1   b  to the through pore  221 - 2 . 
     The second discharge port  222 - 3  is provided to induce the water discharge from the first discharge port  221 - 3  formed in the anode-side member  221  to flow further out to the outside. In addition, it is to be noted that absence of the second discharge port  222 - 3  does not limit the functions described in the present invention. 
       FIG. 5  is a diagram showing the F 5 -F 5  cross section of  FIG. 2 , in which the flowing direction of hydrogen is denoted by D. 
     In  FIG. 5 , the cathode-side pressing member  230  and the anode-side pressing member  240  are not shown for the sake of simple explanation because they do not have influence on the hydrogen flow. 
     Specifically, the hydrogen is introduced to the induction path  222 - 2  through the introduction path  222 - 1  provided in the fuel introducing member  222 . Then, the hydrogen is sprayed from the induction path  222 - 2  toward the anode-side catalyst body of the MEA  210  through the through pore  221 - 2  formed in the anode-side member  221 . 
     The fuel introducing member  222  shown in  FIG. 4  has an outside dimension of 80×70×2 mm, and the induction path  222 - 2  has a depth of 1 mm from the front surface in a front view of the fuel introducing member  222  and has a dimension of 70×53 mm. 
       FIG. 6  is an exploded perspective view of the fuel cell shown in  FIG. 2 , for explaining the flowing direction D of hydrogen. The flow of hydrogen before it reaches the MEA  210  has been described with reference to  FIG. 5 , therefore, redundant descriptions thereof will be omitted. 
     As shown in  FIG. 6 , the hydrogen sprayed onto the MEA  210  is diffused in a radial shape over the surface of the anode-side catalyst body and is supplied to the entire surface of the anode-side catalyst body. 
     According to the embodiment described above, since the fuel is diffused in a radial shape from the center of the anode-side catalyst body, the area where the hydrogen density is uneven becomes smaller than that when the hydrogen is supplied from the introduction port provided at the edge of the anode-side catalyst body. As a result, it is possible to suppress fluctuation of an output voltage and thus to increase an overall output voltage of the fuel cell. 
     In particular, as shown in  FIGS. 5 and 6 , since the hydrogen introduced from the outside is sprayed onto the anode-side catalyst body along a direction of a normal line of the surface of the anode-side catalyst body, the sprayed hydrogen is diffused in a radial shape to the anode-side catalyst body at a substantially uniform flow rate. With this arrangement, compared with the case where the hydrogen introduced from the outside is not moved in the direction of the normal line, when the hydrogen is moved in the direction of the normal line, it is possible to suppress unevenness of the hydrogen density distribution on the anode-side catalyst body and thus to increase the overall output voltage of the fuel cell. 
     In addition, since the introduced hydrogen is temporarily stored in the induction path  222 - 1 , the flow rate of the hydrogen discharged via the induction path  222 - 1  from the through pore  221 - 2  is decelerated to be lower than the flow rate of the hydrogen when it was introduced. With this arrangement, the hydrogen discharged through the through pore  221 - 2  is diffused at substantially uniform pressure with respect to the anode-side catalyst body. For this reason, it is possible to make the hydrogen density distribution on the anode-side catalyst body more uniform and thus to increase an overall output voltage of the fuel cell. 
     Further, since the above-mentioned effect can be obtained when only one introduction port  222 - 1   a  is provided in the fuel introducing member  222 , it is easy to decrease the overall size of the fuel cell system, thereby increasing the volume output density. 
     In addition, since a micro flow path structure is not needed, it is possible to provide easy processing properties. 
     Modified Example 1 
     In the first embodiment, hydrogen is sprayed toward the center of the surface of a single anode-side catalyst body. To the contrary, in a first modified example, hydrogen is sprayed toward the centers of the surfaces of a plurality of anode-side catalyst bodies. The first modified example will be described in detail below. 
       FIG. 7  is a drawing showing a first modified example of the first embodiment of the fuel cell according to the present invention. 
     The fuel cell  400  includes an MEA  410 , a fuel inducing portion  420 , a cathode-side pressing member  430 , and an anode-side pressing member  440 . A gas diffusion member (not shown) and a current collector (not shown) are provided on the anode side and the cathode side of the MEA  410 , respectively. 
     In  FIG. 7 , the fuel cell  400  includes three paired catalyst bodies of a cathode-side catalyst body and an anode-side catalyst body on both sides of the MEA  410 . The fuel cell  400  is an assembly of unit fuel cells (hereinafter, referred to as “cell”) each having a pair of a cathode-side catalyst body and an anode-side catalyst body. 
     Specifically, the MEA  410  includes cathode-side catalyst bodies  412   a ,  412   b , and  412   c  provided on one surface of a solid polymer electrolyte membrane  411  and three anode-side catalyst bodies (not shown) having substantially the same shape as the cathode-side catalyst bodies  412   a ,  412   b , and  412   c  and provided on the other surface. 
     In  FIG. 7 , the MEA  410  has an outside dimension of 80×63×0.03 mm, and the cathode- and anode-side catalyst bodies have a size of 20×53×0.03 mm. 
     Similar to the first embodiment, the fuel inducing portion  420  includes an anode-side member  421  and a fuel introducing member  422 . 
     The cathode-side pressing member  430  and the anode-side pressing member  440  have the same structure and function as those of the cathode-side pressing member  230  and the anode-side pressing member  240  according to the first embodiment shown in  FIG. 2 ; therefore, redundant descriptions thereof will be omitted. 
     In addition, it is preferable that the gas diffusion member (not shown) and the current collector (not shown) have substantially the same shape as the cathode- and anode-side catalyst bodies provided in the MEA  410 . 
       FIG. 8  is a diagram showing the structure of the anode-side member  421  of the fuel cell  400  shown in  FIG. 7 . 
     Similar to the anode-side member  221  of the first embodiment shown in  FIG. 3 , the anode-side member  421  includes a recess portion  421 - 1 , a first through pore (through hole)  421 - 2   b , second through pores (through holes)  421 - 2   a  and  421 - 2   c , and a first discharge port  421 - 3 . 
     The depth and shape of the recess portion  421 - 1  are the same as those of the recess portion  221 - 1  of the first embodiment; however, as shown in  FIG. 8 , convex portions may be formed into a shape that can reinforce the strength of the anode-side member  421  and that does not interfere with the diffusion of a hydrogen rich gas. 
     The first discharge port  421 - 3  has the same structure and function as the first discharge port  221 - 3  of the first embodiment; therefore, redundant descriptions thereof will be omitted. 
     The first through pore  421 - 2   b  and the second through pores  421 - 2   a  and  421 - 2   c  have their centers of gravity located on normal lines of the anode-side catalyst body surface drawn from the centers of the corresponding anode-side catalyst bodies. 
     The outside dimension of the anode-side member  421  shown in  FIG. 8  and the depth of the recess portion  221 - 1  are the same as those of the first embodiment, and the first through pore  421 - 2   b  and the second through pores  421 - 2   a  and  421 - 2   c  have a diameter φ of 6 mm. 
       FIG. 9  is a diagram showing the structure of the fuel introducing member  422  of the fuel cell  400  shown in  FIG. 7 . The fuel introducing member  422  includes an introduction path  422 - 1 , an induction path  422 - 2 , and a second discharge port  422 - 3 . 
     The introduction path  422 - 1  includes an introduction port  422 - 1   a , which is a connecting portion to an external fuel supply portion  100  for introducing hydrogen from the outside, and a terminating port  422 - 1   b , which is an end portion of the introduction path close to the induction path  422 - 2  described after. 
     The introduction port  422 - 1   a  and the terminating port  422 - 1   b  have the sane structure and functions as the introduction port  222 - 1   a  and the terminating port  222 - 1   b  in a basic example of the first embodiment; therefore, redundant descriptions thereof will be omitted. 
     Moreover, detailed descriptions on the second discharge port  422 - 3  are also omitted from the same reason. 
     The induction path  422 - 2  will be described in detail with reference to  FIGS. 10 and 11 . 
     The fuel introducing member  422  shown in  FIG. 9  has substantially the same size as the fuel introducing member  222  of the first embodiment. 
       FIG. 10  is a front view of the fuel introducing member  422  shown in  FIG. 9  as viewed from the anode-side catalyst body.  FIG. 11  is a diagram showing the A-A cross section of  FIG. 10 . 
     In  FIG. 10 , the first through pore  421 - 2   b  and the second through pores  421 - 2   a  and  421 - 2   c  represent the positions of the first through pore  421 - 2   b  and the second through pores  421 - 2   a  and  421 - 2   c  when the anode-side member  421  and the fuel introducing member  422  are assembled with each other and when the fuel introducing member  422  is viewed from the anode-side catalyst body side. 
     Further, the length of the flow path of hydrogen flowing from the terminating port  422 - 1   b  toward the first through pore  421 - 2   b  is denoted by L 2 . Moreover, the lengths of the flow paths of hydrogen flowing from the terminating port  422 - 1   b  toward the second through pores  421 - 2   a  and  421 - 2   c  are denoted by L 1  and L 3 , respectively. 
     Since convex portions are formed in the induction path  422 - 2  of  FIG. 9 , induction paths  422 - 22 ,  422 - 21 , and  422 - 23  are formed to correspond to the first through pore  421 - 2   b , the second through pores  421 - 2   a  and  421 - 2   c . The induction path  422 - 22  forms a first induction path and the induction paths  422 - 21  and  422 - 23  form second induction paths. 
     The induction paths  422 - 21  and  422 - 23  have lengths L 1  and L 3  from the terminating port  422 - 1   b  to the through pores  421 - 2   a  and  421 - 2   c , which are longer than the length L 2  of the induction path  422 - 22 . Specifically, in  FIGS. 10 and 11 , the lengths satisfy the relationship of L 1 =L 3 &gt;L 2 . 
     In  FIG. 11 , S 1 , S 2 , and S 3  represent cross sections of the lower surface of the induction path  422 - 2  corresponding to the induction paths  422 - 21 ,  422 - 22 , and  422 - 23 . 
     The induction path  422 - 2  is structured such that the induction path  422 - 22  has a cross section S 2  smaller than the cross sections S 1  and S 3  of the induction paths  422 - 21  and  422 - 23 . Specifically, in  FIGS. 10 and 11 , the cross sections satisfy the relationship of S 1 =S 3 &gt;S 2 . 
     In addition, the induction paths  422 - 21 ,  422 - 22 , and  422 - 23  only need to have a hydrogen flow path formed therein as long as the above-mentioned relationships are satisfied For example, the induction paths  422 - 21 ,  422 - 22 , and  422 - 23  may be a pipe-shaped tube that connects the terminating port  222 - 1   b  to the respective through pores  421 - 2   a ,  421 - 2   b , and  421 - 2   c.    
     Next, simulation results when hydrogen is introduced to the fuel cell  400  having the fuel inducing portion  420  shown in  FIG. 7  will be described. 
     The simulation was conducted using a hydrogen flow model that since hydrogen is consumed by the anode-side catalyst body during electricity generation in the fuel cell  400 , a predetermined amount of hydrogen is flown out per unit time to the outside from the anode-side catalyst body surface. 
     In this simulation, pure hydrogen was introduced at a flow rate of 6.825E-8 [kg/s]. 
     The hydrogen introduced from the terminating port  422 - 1   b  of the fuel introducing member  422  is supplied through the induction path  422 - 2  and through the first through pore  421 - 2   b  and the second through pores  421 - 2   a  and  421 - 2   c  of the anode-side member  421  to the anode-side catalyst body. 
       FIG. 12  shows the flow rate of hydrogen calculated through simulation, showing the flow rate of hydrogen flowing out from the first through pore  421 - 2   b  and the second through pores  421 - 2   a  and  421 - 2   c.    
     It was confirmed from  FIG. 12  that with the structure of the present invention, even when the pore diameter of the through pores was made identical, the flow rates from the respective through pores were substantially the same with an error of 3.5 percent. 
     In addition, the output voltages of the three cells were substantially the same. Specifically, the output voltages of the cells corresponding to the first through pore  421 - 2   b  and the second through pores  421 - 2   a  and  421 - 2   c  were 0.165 V, 0.6225 V, and 0.621 V, respectively, with an error of 1.2 percent. 
     The length L 2  of the induction path  422 - 22  was smaller than the lengths (L 1  and L 3 ) from the terminating port  422 - 1   b  to the through pores  421 - 2   a  and  421 - 2   c . For this reason, if the induction path  422 - 22  and the induction paths  422 - 21  and  422 - 23  had the same cross sections, most of the hydrogen discharged from the terminating port  422 - 1   b  may have been more easily induced toward the first through pore  421 - 2   b  than the second through pores  421 - 2   a  and  421 - 2   c . In such a case, the amount of hydrogen discharged from the first through pore  421 - 2   b  and the second through pores  421 - 2   a  and  421 - 2   c  may have fluctuated greatly. 
     However, in this modified example, the cross section S 2  of the induction path  422 - 22  is smaller than the cross section (S 1  and S 3 ) of the induction paths  422 - 21  and  422 - 23 . With this structure, it is not likely that most hydrogen flows to the induction path  422 - 22  but substantially the same amount of hydrogen is likely to flow in a distributed manner to the induction paths  422 - 21  to  422 - 23 . Therefore, substantially the same amount of hydrogen can be sprayed onto the respective anode-side catalyst bodies. 
     In addition, since substantially the same amount of hydrogen can be sprayed onto the respective anode-side catalyst bodies, it is possible to suppress the unevenness in the output voltages corresponding to the respective anode-side catalyst bodies. Furthermore, since the respective output voltages of the anode-side catalyst bodies are prevented from becoming extremely lower than other output voltages, it is possible to increase the overall output voltage of the fuel cell. 
     Modified Example 2 
     In the first modified example, the through pores corresponding to the respective anode-side catalyst bodies have the same sizes. To the contrary, in the second modified example, the through pores corresponding to the respective anode-side catalyst bodies are not of the same sizes. The second modified example will be described in detail below. 
       FIG. 13  is a diagram showing the structure of an anode-side member  421 A according to the second modified example of the first embodiment of the fuel cell of the present invention. 
     The anode-side member  421 A is the anode-side member corresponding to the MEA  410  of a planar, multi-electrode structure shown in  FIG. 7  and is a modified example of the anode-side member  421  shown in  FIG. 8 . 
     In this modified example, the fuel introducing member  222  shown in  FIG. 4  is used. The lengths from the terminating port  222 - 1   b  to a first through pore (through hole)  421 - 5   b  and second through pores (through holes)  421 - 5   a  and  421 - 5   c  of the anode-side member  421 A are denoted by Lb, La, and Lc. Similar to the first modified example, the lengths satisfy the relationship of La=Lc&gt;Lb. 
     Furthermore, the pore diameter φDb of the first through pore  421 - 5   b  and the pore diameters φDa and φDc of the second through pores  421 - 5   a  and  421 - 5   c  satisfy the relationship of Da=Dc&gt;Db. 
     In the second modified example of the first embodiment shown in  FIG. 13 , the pore diameters are set such that Da=Dc=4 mm and Db=2 mm. 
     Next, simulation results when hydrogen is introduced to a fuel cell having a fuel inducing portion formed by the fuel introducing member  222  and the anode-side member  421 A will be described. 
     Similar to the calculation performed in the first modified example of the first embodiment, pure hydrogen was introduced at a flow rate of 6.825E-8 [kg/s]. The hydrogen flow path is the same as that of the first modified example; therefore, redundant descriptions thereof will be omitted. 
       FIG. 14  shows the flow rate of hydrogen calculated through simulation, showing the flow rate of hydrogen flowing out from the first through pore  421 - 5   b  and the second through pores  421 - 5   a  and  421 - 5   c.    
     It was confirmed from  FIG. 14  that with the structure of the second modified example of the first embodiment, the flow rates from the respective through pores were substantially the same with an error of 2 percent. 
     The feasibility of the simulation and the correspondence between the unevenness of the hydrogen flow rate and the unevenness of the output voltage were described in connection with the first modified example of the first embodiment; therefore, redundant descriptions thereof will be omitted. 
     The first through pore  421 - 5   b  is disposed closer to the terminating port  222 - 1   b  than the second through pores  421 - 5   a  and  421 - 5   c . For this reason, if the first through pore  421 - 5   b  and the second through pores  421 - 5   a  and  421 - 5   c  had the same sizes, most of the hydrogen discharged from the terminating port  222 - 1   b  may have been more easily induced toward the first through pore  421 - 5   b  than the second through pores  421 - 5   a  and  421 - 5   c . In such a case, the amount of hydrogen discharged from the first through pore  421 - 5   b  and the second through pores  421 - 5   a  and  421 - 5   c  may have fluctuated greatly. 
     However, in this modified example, the size of the first through pore  421 - 5   b  is smaller than the sizes of the second through pores  421 - 5   a  and  421 - 5   c . With this structure, it is not likely that most hydrogen is discharged from the first through pore  421 - 5   b  but substantially the same amount of hydrogen is likely to be discharged in a distributed manner from the first through pore  421 - 5   b  and the second through pores  421 - 5   a  and  421 - 5   c . Therefore, substantially the same amount of hydrogen can be sprayed onto the respective anode-side catalyst bodies. 
     In addition, since substantially the same amount of hydrogen can be sprayed onto the respective anode-side catalyst bodies, it is possible to suppress the unevenness in the output voltages corresponding to the respective anode-side catalyst bodies. Furthermore, since the respective output voltages of the anode-side catalyst bodies are prevented from becoming extremely lower than other output voltages, it is possible to increase the overall output voltage of the fuel cell. 
     Embodiment 2 
     In the fuel inducing portion of the first embodiment, hydrogen is introduced toward the center of the surface of a single anode-side catalyst body. To the contrary, in a second embodiment, hydrogen is induced toward plural locations of the surface of a single anode-side catalyst body. The second embodiment will be described in detail below. 
       FIG. 15  is a diagram showing the structure of an anode-side member  221 A according to the second embodiment of a fuel cell of the present invention. 
     The anode-side member  221 A is a modified example of the anode-side member  221  of the fuel cell  200  shown in  FIG. 2 . The anode-side member  221 A includes a recess portion  221 - 1  on a side where an anode-side catalyst body is disposed. A plurality of through pores  221 - 4   a ,  221 - 4   b , and  221 - 4   c  are formed in the recess portion  221 - 1 . 
     The anode-side member  221 A has a triangular surface  221 - 5  (polygonal surface) formed by the lines passing through the above-mentioned three through pores. In a front view of the anode-side member  221 A as viewed from the cathode side, the triangular surface  221 - 5  is disposed at a position overlapping the surface of the anode-side catalyst body. 
     In this embodiment, the above-mentioned three through pores are arranged such that a normal line of the anode-side catalyst body surface passing through the center (the center of gravity) of the anode-side catalyst body passes through the inner side of the triangular surface  221 - 5 . 
     According to this embodiment, since a plurality of through pores is provided, an overall opening area can be increased larger than that when only one through pore is provided. With this arrangement, the flow rate of the hydrogen discharged from the through pores can be decelerated to be lower than that when only one through pore is provided. Therefore, the hydrogen can be sprayed at substantially uniform pressure with respect to the anode-side catalyst body. Accordingly, it is possible to make the hydrogen density distribution on the anode-side catalyst body more uniform. 
     In additions the triangular surface  221 - 5  is disposed at a position overlapping the center (the center of gravity) of the surface of the anode-side catalyst body in a front view of the anode-side body  221 A as viewed from the cathode side. For this reason, the hydrogen discharged from the respective through pores can be sprayed with more uniform pressure with respect to the surface of the anode-side catalyst body. 
     Further, the through pores  221 - 4   a ,  221 - 4   b , and  221 - 4   c  may have arbitrary pore sizes; however, it is preferable that they are substantially of the same circular shape. The above-mentioned normal line may pass through the center of a circumscribed circle of the triangular surface  221 - 5 . 
     In addition, in this embodiment, three through pores are provided; however, two through pores may be provided, and in such a case, it is preferable that the above-mentioned normal line passes through the middle point of the distance between the centers of the two through pores. 
     Furthermore, in this embodiment, the fuel introducing member may have a structure having a single induction path, similar to the fuel introducing member  222  described in the first embodiment, it is preferable that the fuel introducing portion has induction paths provided for the respective through pores and that the cross sections of the induction paths and the distances from the introduction path to the respective through pores satisfy the relationship described in the first modified example of the first embodiment. 
     Modified Example 1 
     In the second embodiment, the anode-side member  221 A includes the triangular surface  221 - 5  formed by the lines passing through the three through pores. To the contrary, in a first modified example, an anode-side member  221 B has a rectangular surface  221 - 7  formed by the lines passing through four through pores. The first modified example will be described in detail below. 
       FIG. 16  is a diagram showing the structure of the anode-side member  221 B according to the first modified example of the second embodiment. 
     The anode-side member  221 B includes through pores  221 - 6   a ,  221 - 6   b ,  221 - 6   c , and  221 - 6   d.    
     In a front view of the anode-side member  221 B as viewed from the cathode side, the rectangular surface  221 - 7  is disposed at a position overlapping the surface of the anode-side catalyst body. 
     In this modified example, the above-mentioned four through pores are arranged such that a normal line of the anode-side catalyst body surface passing through the center (the center of gravity) of the anode-side catalyst body passes through the inner side of the rectangular surface  221 - 7 . 
     The through pores  221 - 6   a ,  221 - 6   b ,  221 - 6   c , and  221 - 6   d  may have arbitrary pore sizes; however, it is preferable that they are substantially of the same circular shape. The above-mentioned normal line may pass through the center of gravity of the rectangular surface  221 - 7 . 
     In addition, in this modified example of the present embodiment, four through pores are provided; however, five or more through pores may be provided. Further, even in the case where five or more through pores are provided, the positional relationship of the through pores is the same as that described above; therefore, redundant descriptions thereof will be omitted. 
     Further, when the centers of the through pores are connected to form a polygonal surface having a point having a vertex angle equal to or greater than 180 degrees, it is preferable that the through pores are arranged such that all the remaining points of the polygonal surface have a vertex angle equal to or smaller than 180 degrees and that the center of gravity of an arbitrary polygonal surface containing all the through pores passes through the above-mentioned normal line. 
     In this modified example of the present embodiment, the induction path of the fuel introducing member has the same shape as the second embodiment; therefore, redundant descriptions thereof will be omitted. 
     According to this embodiment, since a plurality of through pores is provided, an overall opening area can be increased larger than that when only one through pore is provided. With this arrangement, the flow rate of the hydrogen discharged from the through pores can be decelerated to be lower than that when only one through pore is provided. Therefore, the hydrogen can be sprayed at substantially uniform pressure with respect to the anode-side catalyst body. Accordingly, it is possible to make the hydrogen density distribution on the anode-side catalyst body more uniform. 
     Specifically, since four through pores are provided, compared with the case where three through pores are provided, the hydrogen discharged from the respective through pores can be sprayed with more uniform pressure with respect to the anode-side catalyst body. 
     Modified Example 2 
     In the second embodiment, hydrogen is induced toward plural locations of the surface of a single anode-side catalyst body. To the contrary, in a second modified example, hydrogen is induced toward plural locations of the respective surfaces of plural anode-side catalyst bodies. The second modified example will be described in detail below. 
       FIG. 17  is a diagram showing the structure of an anode-side member  421 B and the MEA  410  according to the second modified example of the second embodiment. 
     The anode-side member  421 B includes nine through pores (through holes)  421 - 4   a ,  421 - 4   b ,  421 - 4   c ,  421 - 4   d ,  421 - 4   e ,  421 - 4   f ,  421 - 49 ,  421 - 4   h , and  421 - 4   i  so that three through pores correspond to each of the anode-side catalyst bodies provided to the MEA  410 . 
     Specifically, in  FIG. 17 , the through pores  421 - 4   a ,  421 - 4   d , and  421 - 4   g  are provided to correspond to the anode-side catalyst body that is opposed to the cathode-side catalyst body  412   a  via the MEA  410 . 
     Further, the through pores  421 - 4   b ,  421 - 4   e , and  421 - 4   h  are provided to correspond to the anode-side catalyst body that is opposed to the cathode-side catalyst body  412   b  via the MEA  410 . 
     Furthermore, the through pores  421 - 4   c ,  421 - 4   f , and  421 - 4   i  are provided to correspond to the anode-side catalyst body that is opposed to the cathode-side catalyst body  412   c  via the MEA  410 . 
     In this modified example, the three through pores corresponding to a single anode-side catalyst body are arranged in a row; however, it is to be noted that the invention is not limited to this. For example, the three through pores corresponding to a single anode-side catalyst body may be disposed at positions as shown in  FIG. 15 . 
     Further, the three through pores may be arranged at equal intervals along a straight line. In addition, it is preferable that among the plural through pores arranged at equal intervals, the central through pore is disposed at a position that the above-mentioned normal line passes through. 
     In this way, since the fuel supplied from the outside is induced toward plural locations of the respective surfaces of the plural anode-side catalyst bodies, it is possible to make the fuel density distribution in the anode-side catalyst body surface of each cell more uniform and thus to make the fuel supply amount uniform between the cells. With this arrangement, it is possible to suppress unevenness in an output voltage between the cells and thus to increase an overall output voltage of the fuel cell. 
     Embodiment 3 
       FIG. 18  is a diagram showing the structure of a third embodiment of the fuel cell of the present invention. 
     In  FIG. 18 , a fuel cell  500  includes an MEA  210 , a fuel inducing portion  510 , a cathode-side pressing member (not shown), an anode-side pressing member (not shown), a gas diffusion member (not shown), and a current collector. 
     The MEA  210  includes a solid polymer electrolyte membrane  211 , a cathode-side catalyst body  212  and an anode-side catalyst body (not shown) disposed on opposite surfaces of the solid polymer electrolyte membrane. 
     The fuel inducing portion  510  includes an anode-side member  511  and a fuel introducing member  512 . 
     In the first and second embodiments, the fuel introducing member is disposed at a side opposite to the side at which the anode-side catalyst body is opposed to the solid polymer electrolyte membrane  211  so as to be in parallel to the anode-side member via the anode-side member. 
     To the contrary, in this embodiment, the fuel introducing member  512  can be disposed at an arbitrary position adjacent to the anode-side member  511 . Specifically, the fuel introducing member  512  can be disposed at a position where the anode-side member  511  is at the substantially same surface as the fuel introducing member  512 . 
     The anode-side member  511  includes a first plate member  511 - 1 , a supply port  511 - 2 , an introduction path  511 - 3 , and a connecting port  511 - 4 . 
     The supply port  511 - 2  is provided to supply hydrogen to the anode-side catalyst body. The supply port  511 - 2  is not penetrated but is an opening formed at a side where the first plate member  511 - 1  is opposed to the anode-side catalyst body. The supply port  511 - 2  is disposed on a normal line of the anode-side catalyst body surface and is also disposed on a line passing through the center of the anode-side catalyst body. 
     The introduction port  511 - 3  is provided to induce the hydrogen introduced from the connecting port  511 - 4  toward the supply port  511 - 2 . The introduction port  511 - 3  is formed into a tube shape along the surface direction of the first plate member  511 - 1 . The connecting port  511 - 4  is connected to the fuel introducing member  512 . 
     It is to be noted that only one supply port  511 - 2  may be provided for a single anode-side catalyst body as shown in  FIG. 18  and plural supply ports may be provided for a single anode-side catalyst body. 
     Further, when plural supply ports are provided, it is preferable that for a supply port  511 - 2 A disposed at a small distance from the connecting port  511 - 4 , the cross section of an introduction path  511 - 3 A connected to the supply port  511 - 2 A is small, while for a supply port  511 - 2 B disposed at a large distance from the connecting port  511 - 4 , the cross section of the introduction path  511 - 3 B connected to the supply port  511 - 2 B is large. 
     Alternatively, the introduction paths from the connecting port  511 - 4  to the respective supply ports may be formed to have the same cross sections, and the supply port  511 - 2 A disposed at a small distance from the connecting port  511 - 4  may be formed to have a small area while the supply port  511 - 2 B disposed at a large distance from the connecting port  511 - 4  may be formed to have a large area. 
     The fuel introducing member  512  includes a second plate member  512 - 1 , an induction path  512 - 2 , and an introduction port  512 - 3 . 
     The introduction port  512 - 3  is connected to an external fuel supply portion  100  and supplies hydrogen to the induction path  512 - 2 . 
     The introduction port  512 - 3  may be provided at an arbitrary position of the second plate member  512 - 1 . In addition, the introduction port  512 - 3  may have an arbitrary shape. When connecting the anode-side member  511  and the fuel introducing member  512 , the introduction port  512 - 3  is preferably constructed such that it is opened in an axial direction different from a normal line of the connecting surface. 
     It is to be noted that the induction path  512 - 2  is a space formed in the second plate member  512 - 1  and may function as a buffer when hydrogen is supplied. That is, the induction path  512 - 2  may be constructed to decelerate the speed of introduced hydrogen to be lower than that when it was introduced. 
     By having the above-described structure, the position of the fuel introducing member  512  can be set arbitrarily, thereby improving the degree of freedom in designing a layout of the fuel introducing member  512  and thus contributing to downsizing the thickness of the fuel cell. 
     Other Embodiments 
     Hereinabove, examples of the present invention have been described by way of specific examples thereof. However, it is to be noted that the present invention is not limited to these example but various modifications in design can be appropriately made to the detailed structure of the above-described embodiments. 
     The detailed structures shown in the embodiments and the modified examples may be combined with each other. The operations and effects of the embodiments are merely enumerations of the best feasible operations and effects incurred from the present invention, and the operation and effect of the present invention are not limited to those described in the embodiments. 
     In all of the embodiments described above, the fuel is not limited to hydrogen and any fuel such as methanol solution can be used as long as it allows extracting protons and electrons from a catalyst body of an MEA. 
     As an effect of all of the embodiments described above, in particular, in a fuel cell having a dead-end structure with no outlet port, only hydrogen necessary for electricity generation is supplied; therefore, compared with the conventional technology (flow structure) in which the hydrogen density in the vicinity of the introduction port is higher than the hydrogen density at a portion on the anode-side catalyst body disposed farthest from the introduction port, with the structure of the present invention, it is possible to provide a more uniform hydrogen density distribution and thus to contribute to increasing the overall output of the fuel cell. 
     Further, the dead-end structure as used in this embodiment refers to a structure in which the fuel inducing portion induces the introduced fuel only toward the anode-side catalyst body and in which the hydrogen is not induced to the outside. On the other hand, the flow structure refers to a structure in which the fuel inducing portion induces the introduced fuel to both the anode-side catalyst body and the outside. 
     INDUSTRIAL APPLICABILITY 
     According to the fuel cell of the present invention, it is possible to suppress unevenness in a hydrogen density distribution and to increase an output voltage.