text: the invention summarized above and defined by the enumerated claims may be better understood by referring to the following detailed description , which should be read with reference to the accompanying drawings . this detailed description of particular preferred embodiments , set out below to enable one to build and use particular implementations of the invention , is not intended to limit the enumerated claims , but to serve as particular examples thereof . [ 0044 ] fig1 is a diagram showing an exploded perspective view of a fuel cell unit manufactured by a method in accordance with the first embodiment of the present invention . the fuel cell unit 10 includes a membrane electrode assembly 12 , and a cathode side separator 14 and an anode side separator 16 , which hold the membrane electrode assembly 12 . a plurality of the fuel cell units 10 may be stacked to produce , for example , a fuel cell stack used for a vehicle . the membrane electrode assembly 12 includes a solid polymer electrolyte membrane 18 , and a cathode side catalytic layer 20 and an anode side catalytic layer 22 which are disposed so as to sandwich the solid polymer electrolyte membrane 18 . also , a cathode side gas diffusion layer 24 and an anode side gas diffusion layer 26 are disposed outside of the cathode side catalytic layer 20 and the anode side catalytic layer 22 , respectively . the cathode side catalytic layer 20 together with the cathode side gas diffusion layer 24 forms a cathode 25 . similarly , the anode side catalytic layer 22 together with the anode side gas diffusion layer 26 forms an anode 27 . as shown in fig1 the solid polymer electrolyte membrane 18 has a marginal portion 18 a , i . e ., an area outside of the two - dotted line in the solid polymer membrane portion 18 a , i . e ., an area outside of the two - dotted line in the solid polymer membrane anode side catalytic layer 22 when disposed so as to sandwich the solid polymer electrolyte membrane 18 . a liquid sealant s , which is applied to the outer peripheral portion of the cathode side separator 14 and that of the anode side separator 16 , makes direct contact with a side ( i . e ., a surface ) of the marginal portion 18 a . the liquid sealant s will be with a side ( i . e ., a surface ) of the marginal portion 18 a . the liquid sealant s will be the cathode side separator 14 , as shown in fig1 includes an inlet side fuel gas opening 36 a for allowing a fuel gas , such as a gas containing hydrogen , to pass through , at the upper left end close to the edge thereof , and an inlet side oxidant gas opening 38 a for allowing an oxidant gas , such as a gas containing oxygen , or air , to pass through , at the upper right end close to the edge thereof . also , the cathode side separator 14 includes an inlet side cooling medium opening 40 a which allows a cooling medium , such as pure water , ethylene glycol , or oil , to pass through at the left end at the middle in the vertical direction , and an outlet side cooling medium opening 40 b which allows the used cooling medium to pass through at the right end at the middle in the vertical direction . moreover , the cathode side separator 14 includes an outlet side fuel gas opening 36 b for allowing the fuel gas to pass through at the lower right end close to the edge thereof , and an outlet side oxidant gas opening 38 b for allowing the oxidant gas to pass through at the lower left end close to the edge thereof . in this embodiment , the outlet side fuel gas opening 36 b and the outlet side oxidant gas opening 38 b are disposed so as to be diagonal with respect to the inlet side fuel gas opening 36 a and the inlet side oxidant gas opening 38 a , respectively . as shown in fig1 a plurality of independent first oxidant gas channels 42 are formed on a surface 14 a of the cathode side separator 14 opposite the cathode side catalytic layer 20 . the first oxidant gas channels 42 start in the vicinity of the inlet side oxidant gas opening 38 a , and run horizontally while meandering downward in the direction of gravity . the first oxidant gas channels 42 merge into a plurality of second oxidant gas channels 44 , and the second oxidant gas channels 44 end in the vicinity of the outlet side oxidant gas opening 38 b . the cathode side separator 14 includes first oxidant gas connecting passages 46 which passes through the cathode side separator 14 , whose ends are connected to the inlet side oxidant gas opening 38 a on a surface 14 b opposite the surface 14 a , and whose other ends are connected to the first oxidant gas channels 42 on the surface 14 a . also , the cathode side separator 14 includes second oxidant gas connecting passages 48 which passes through the cathode side separator 14 , whose ends are connected to the outlet side oxidant gas opening 38 b on the surface 14 b , and whose other ends are connected to the second oxidant gas channels 44 on the surface 14 a . in addition , the anode side separator 16 also includes an inlet side fuel gas opening 36 a , an inlet side oxidant gas opening 38 a , an inlet side cooling medium opening 40 a , an outlet side cooling medium opening 40 b , an outlet side fuel gas opening 36 b , and an outlet side oxidant gas opening 38 b , at both ends close to the edges thereof , in a manner similar to the cathode side separator 14 . as shown in fig2 a plurality of independent first fuel gas channels 60 are formed on a surface 16 a of the anode side separator 16 in the vicinity of the inlet side fuel gas opening 36 a . the first fuel gas channels 60 run horizontally while meandering downward in the direction of gravity , and merge into three second fuel gas channels ( not shown in the figure ). the second fuel gas channels end in the vicinity of the outlet side fuel gas opening 36 b . the anode side separator 16 includes first fuel gas connecting passages 64 which connect the inlet side fuel gas opening 36 a on the surface 16 b to the first fuel gas channels 60 , and second fuel gas connecting passages ( not shown in the figure ) which connect the outlet side fuel gas opening 36 b on the surface 16 b to the second fuel gas channels 62 . the first fuel gas connecting passages 64 and the second fuel gas connecting passages are formed so as to pass through the anode side separator 16 . a plurality of main channels 72 a and 72 b which function as cooling medium channels are formed on the surface 16 b of the anode side separator 16 , within the area enclosed by the liquid sealant s , which will be described later , and close to the inlet side cooling medium opening 40 a and the outlet side cooling medium opening 40 b . also , a plurality of branch channels 74 branch off from the main channels 72 a and 72 b are disposed so as to extend in the horizontal direction . the anode side separator 16 includes first cooling medium connecting passages 76 which connect the inlet side cooling medium opening 40 a to the main channels 72 a , and second cooling medium connecting passages 78 which connect the outlet side cooling medium opening 40 b to the main channels 72 b . the first cooling medium connecting passages 76 and the second cooling medium connecting passages 78 pass through the anode side separator 16 . in this embodiment , a groove portion 28 is formed on the surface 16 a of the anode side separator 16 a ( i . e ., an area of the separator 16 a corresponding to the marginal portion 18 a ), which holds the solid polymer electrolyte membrane 18 , opposite the anode side catalytic layer 22 at a position corresponding to the marginal portion 18 a of the solid polymer electrolyte membrane 18 . the liquid sealant s is applied to the groove portion 28 . also , a groove portion 30 is formed around each of the inlet side fuel gas opening 36 a , the inlet side oxidant gas opening 38 a , the inlet side cooling medium opening 40 a , the outlet side cooling medium opening 40 b , the outlet side fuel gas opening 36 b , and the outlet side oxidant gas opening 38 b , which are formed on the surface 16 a of the separator 16 . the liquid sealant s is also applied to the groove portion 30 . moreover , the groove portions 28 and 30 are formed on the surface 14 a of the cathode side separator 14 , which holds the membrane electrode assembly 12 together with the anode side separator 16 , opposite the cathode side catalytic layer 20 , at a position corresponding to the groove portions 28 and 30 , respectively , on the surface 16 a of the anode side separator 16 . the liquid sealant s is also applied to each of the groove portions 28 and 30 . accordingly , as shown in fig2 the liquid sealant s applied to the groove portions 28 and 30 on the cathode side separator 14 and the anode side separator 16 which hold the membrane electrode assembly 12 , respectively , seal around the membrane electrode assembly 12 by directly contacting with the marginal portion 18 a at positions sandwiching the marginal portion 18 a as for the liquid sealant s used for the groove portion 28 , and seal around the openings 36 a , 36 b , 38 a , 38 b , 40 a , and 40 b by directly contacting with each other as for the liquid sealant s used for the groove portion 30 . a groove portion 34 which surrounds the branch channels 74 is formed on the surface 16 b of the anode side separator 16 at a position opposite the surface 14 b of the cathode side separator 14 when a plurality of the fuel cell units 10 are stacked . the liquid sealant s is also applied to the groove portion 34 . also , a groove portion 35 is formed around each of the inlet side fuel gas opening 36 a , the inlet side oxidant gas opening 38 a , the inlet side cooling medium opening 40 a , the outlet side cooling medium opening 40 b , the outlet side fuel gas opening 36 b , and the outlet side oxidant gas opening 38 b on the surface 16 b of the anode side separator 16 . the liquid sealant s is also applied to the groove portion 35 . the groove portions 35 around the inlet side fuel gas opening 36 a and the outlet side fuel gas opening 36 b are formed so as to surround the first fuel gas connecting passage 64 and the second fuel gas connecting passage 66 , respectively . also , the groove portions 35 around the inlet side oxidant gas opening 38 a and the outlet side oxidant gas opening 38 b are formed so as to surround the inlet side oxidant gas opening 38 a and the outlet side oxidant gas opening 38 b , respectively , on the surface 14 b of the cathode side separator 14 . accordingly , when the fuel cell units 10 are stacked and the surface 14 b of the cathode side separator 14 contacts the surface 16 b of the anode side separator 16 , the liquid sealant s of the anode side separator 16 arranged around the inlet side fuel gas opening 36 a , the inlet side oxidant gas opening 38 a , the inlet side cooling medium opening 40 a , the outlet side cooling medium opening 40 b , the outlet side fuel gas opening 36 b , the outlet side oxidant gas opening 38 b , and the branch channels 74 are in contact with the surface 14 b of the cathode side separator 14 , thereby ensuring watertightness between the cathode side separator 14 and the anode side separator 16 . in this embodiment , the above - mentioned liquid sealant s may be made of a thermosetting type fluoride material or a thermosetting type silicone , and has a viscosity of a certain degree by which the cross - sectional shape thereof will not change in an applied state , and be cured ( or solidified ) after the application while maintaining a certain degree of elasticity . in addition , the liquid sealant s is made of a material which is capable of absorbing dimensional errors at sealing portions , i . e ., non - uniformity in the thickness hmea of the membrane electrode assembly 12 and in the thickness of the cathode side and the anode side separators 14 and 16 , by being squeezed in the groove portions 28 , 30 , 34 , and 35 after the application , and makes uniform the compression amount in a load applied state after being cured . next , main steps of a method for manufacturing the fuel cell unit 10 having the above - mentioned structure , and a method for manufacturing a fuel cell stack which is produced by stacking a plurality of the fuel cell units 10 according to an embodiment of the present invention will be described with reference to fig3 through 9 . first , the cathode side separator 14 and the anode side separator 16 having the above - mentioned configuration are prepared , and the liquid sealant s is applied to each of the groove portions 28 and 30 formed on the separators 14 and 16 ( refer to fig3 ). note that the cross - sectional shape of the liquid sealant s applied is substantially circular as shown in fig4 and this shape is maintained . next , the membrane electrode assembly 12 constructed in advance is prepared and the membrane electrode assembly 12 is disposed between the cathode side separator 14 and the anode side separator 16 , and then placed between a compression jig 82 as shown in fig5 . in fig5 the numeral 86 indicates supporting jigs which support the outer periphery portion of the membrane electrode assembly 12 while positioning the membrane electrode assembly 12 with respect to the cathode side and anode side separators 14 and 16 in the in - plane direction . after this , a temporary assembly of a fuel cell is carried out by closing an upper and a lower part of the compression jig 82 to hold the membrane electrode assembly 12 by the cathode side and the anode side separators 14 and 16 so that the liquid sealant s applied to the groove portions 28 on both separators 14 and 16 makes direct contact to the marginal portion 18 a of the solid polymer electrolyte membrane 18 at a position the marginal portion 18 a of the solid polymer electrolyte membrane 18 at a position direct contact with each other . the term temporary assembly means an assembly of a fuel cell to reach a state in which a low degree of load is applied thereon so that the thickness hmea of the membrane electrode assembly 12 is made uniform in the in - plane direction . during the temporary assembly , the liquid sealant s is squeezed in the groove portions 28 and 30 , and absorbs errors in the sealing portions , i . e ., the non - uniformity in thickness hmea of the membrane electrode assembly 12 and in the thickness of the cathode side and anode side separators 14 and 16 . in this manner , the compression amount , i . e ., the tightening margin , of the liquid sealant s at each of the sealing portions is made uniform over the entire fuel cell stack even when compressed in the stacking direction by using bolts 92 after the fuel cell units are stacked . this will be described later . after this , the temporary assembly in which the membrane electrode assembly 12 is sandwiched by the cathode side and the anode side separators 14 and 16 , is heated together with the compression jig 82 in an oven so that the liquid sealant s is cured while the above - mentioned load is applied thereto . after the compression jig 82 is separated from the temporary assembly and the assembly is cooled , a fuel cell unit 10 having the above - mentioned configuration and constant tightening margin of the liquid sealant s is obtained even if the thickness of the membrane electrode assembly 12 is not uniform in the in - plane direction ( refer to fig6 ). then , the liquid sealant s is applied to the groove portions 34 and 35 formed on the surface 16 b of the anode side separator 16 of the fuel cell unit 10 obtained by the procedure explained above ( refer to fig7 ), and a process is repeated in which the surface 14 b of the cathode side separator 14 of another fuel cell unit 10 also obtained via the above procedure is placed on the surface 16 b so that the fuel cell units 10 are sequentially stacked on an end plate 90 ( refer to fig8 ). after a predetermined number of the fuel cell units 10 are stacked , another end plate ( not shown in the figure ) is placed on top and the plates are tightened by using the bolts 92 to produce a fuel cell stack . more specifically , when the end plates are tightened by using the bolts 92 , a compression load is applied in the stacking direction , i . e ., the direction reducing the distance between the end plates 90 . accordingly , surface pressure which is sufficient for suppressing the increase in the internal resistance of the contact resistance is generated at each of the stacking surfaces in and between the fuel cell units 10 . during that time , the liquid sealant s in the groove portions 28 , 30 , 34 , and 35 are squeezed , and the seal compression amount δh at each sealing portion is made constant regardless of the non - uniformity in thickness h mea of the membrane electrode assembly 12 and in the thickness of the cathode side and the anode side separators 14 and 16 ( refer to fig9 ). that is , as shown in fig1 , when the thickness h mea of the membrane electrode assembly 12 differs by δh mea with respect to the standard thickness h mea , the non - uniformity δh mea of the thickness h mea is directly reflected on the seal compression amount δh if a solid seal is used as in conventional techniques . however , when liquid sealant s is used as in the embodiments of the present invention , the non - uniformity δh mea is not reflected on the seal compression amount δh ′ since the non - uniformity δh mea is absorbed during the temporary assembly . accordingly , the tightening margins are made constant according to the embodiments of the present invention . in this manner , as shown in the graph in fig1 , the non - uniformity a fs ′ of the seal load fs ( expressed by a dashed line in the graph ), which may be expressed by the distance between points of intersection , which are present on the threshold value of a surface load f of the membrane electrode assembly 12 required for obtaining the above - mentioned degree of the seal surface pressure , formed by the surface load curve ( expressed by a two - dotted line in the graph ) of the membrane electrode assembly 12 having a standard thickness h mea , and by the surface load curve ( expressed by a solid line in the graph ) of the membrane electrode assembly 8 having a thickness h mea which is different from the standard thickness by δh mea , can be significantly reduced as compared with the non - uniformity δfs obtained when a solid seal is used as in conventional techniques . as explained above , by using the methods for producing fuel cell units 10 and for producing fuel cell stacks according to the embodiments of the present invention , the seal surface pressure acting on sealing portions is made uniform and an excellent sealing property is maintained due to excellent follow - up of the liquid sealant s for the dimensional errors . accordingly , it becomes possible to produce the fuel cell unit 10 and the fuel cell stack which are capable of exerting a desired power generation property . also , according to the present invention , since a strict control of the dimension , especially in the thickness direction , becomes unnecessary for the membrane electrode assembly 12 , and the cathode side and the anode side separators 14 and 16 due to the excellent follow - up property of the liquid sealant s as mentioned above , it becomes possible to significantly reduce the manufacturing cost . moreover , since the surface load between the fuel cell units 10 is made constant , the thickness of each of the separators 14 and 16 may be decreased . accordingly , the size and weight of the fuel cell unit 10 and the fuel cell stack can be reduced , and a fuel cell stack which is especially suitable for a vehicle in which the size of available space is restricted and the thickness of each of the separators 14 and 16 must be minimized as much as possible , can be produced . having thus described exemplary embodiments of the invention , it will be apparent that various alterations , modifications , and improvements will readily occur to those skilled in the art . such alterations , modifications , and improvements , though not expressly described above , are nonetheless intended and implied to be within the spirit and scope of the invention . accordingly , the foregoing discussion is intended to be illustrative only ; the invention is limited and defined only by the following claims and equivalents thereto .