an illustrative embodiment of the present invention relates to an mea having significantly enhanced power density per unit area of the mea relative to known high temperature pem meas , and a corresponding method of making more specifically , current high temperature pem meas have a power density per unit area of , for example , 120 - 150 mw / cm 2 at 0 . 67v with ambient pressure h 2 / air operating at 180 ° c . the mea of the present invention has a power density per unit area of about 200 mw / cm 2 at 0 . 67v with ambient pressure h 2 / air operating at 180 ° c . this is achieved by co - depositing with the catalyst particles an additive ( or additives ) having desired reactionary properties as described herein into a layer when forming the mea . the additive material ( s ) can also be a nano - structural material of an organic or inorganic acid , or acid salt , phosphates , sulfates , carbides , silicates , and the like , in addition to other materials further described herein , and their equivalents . fig1 is an expanded view of a fuel cell stack 20 in accordance with one example embodiment of the present invention . first and second compression plates 22 , 24 form the top and bottom plates . adjacent the compression plates 22 , 24 are current collector plates 26 , 28 . an insulator laminate can be provided between the compression plates 22 , 24 and the current collector plates 26 , 28 as would be well understood by one of skill in the art . adjacent the collector plates are a plurality of support plates and meas . as shown in the figure , there is a first support plate , 30 , a second support plate 32 , and a third support plate 34 . sandwiched between each support plate is an mea 10 . as shown in the figure , there is a first mea 10 a , and a second mea 10 b . the support plate 30 , 32 , 34 includes a first seal 50 a and a second seal 50 b , each positioned on opposing sides of a supporting plate 40 . the first and second seals 50 a , 50 b , are adhered to the supporting plate 40 to form each of the first , second , and third support plates 30 , 32 , 34 . the seal 50 a , 50 b is affixed on each side of the support plate 30 , 32 , 34 , and is configured for sealing against the mea 10 ( 10 a , 10 b ), or the current collector plates 26 , 28 with compression . those of skill in the art will appreciate that other configurations of fuel cell stacks exist . as such , the present invention is by no means limited to the illustrative embodiment shown in fig1 . rather , any fuel cell stack making use of an mea 10 ( 10 a , 10 b ) as described herein is anticipated for use in accordance with the present invention . the description provided herein provides an illustrative example of a membrane electrode assembly having an additive ( or additives ) co - deposited with a catalyst thereon , and corresponding method of manufacture , according to the present invention . although the present invention will be described with reference to the example embodiment , it should be understood that many alternative forms can embody the present invention . one of skill in the art will additionally appreciate different ways to alter the parameters of the embodiments disclosed , such as the size , shape , or type of elements or materials , in a manner still in keeping with the spirit and scope of the present invention . two conventional methodologies for membrane electrode assembly ( mea ) fabrication are : ( a ) application of the catalyst particles on a conductive support surface or electrode and then bonding the catalyzed electrode with pem surface to create the membrane - electrode interface , and ( b ) application of the catalyst particles on the pem surface directly to fabricate the catalyst - coated membrane ( ccm ) and then attaching or bonding the conducting electrode material ( electrode with gas diffusion layer , gdl ) with the ccm surface to form the mea . with respect to the present invention , the process of catalyst - coated membrane ( ccm ) fabrication is relatively more cumbersome using phosphoric acid infused high temperature proton exchange membrane ( ht pem ). as such , manufacture of the mea in accordance with the present invention can be done in a more similar fashion to the first method described above , namely , application of catalyst particles on a conductive surface or electrode , which is then bonded to the proton exchange membrane ( pem ) surface to create the mea . however , the method of manufacture in accordance with the present invention differs from the conventional method . in accordance with the present invention , an additive ( or additives ) is co - deposited with the catalyst particles onto the electrode surface using any suitable coating techniques ( e . g ., spray - coating or printing using the catalyst ink ). one of skill in the art will appreciate that there are multiple different coating technologies that can be used to apply the additive and catalyst particles to the electrode . as such , the present invention is by no means limited only to those described herein . rather , it is the co - depositing of the additive ( s ) with the catalyst that is relevant , and any coating method capable of such co - depositing methodology is anticipated for use with the present invention . the result of the manufacturing process is illustrated in fig2 , which shows a cross - sectional view of an mea 10 , in accordance with one embodiment of the present invention . the mea 10 is formed of a proton exchange membrane ( pem ) 70 . an electrode support layer 60 , typically formed of carbon - based material ( e . g ., carbon fabric or paper ), is placed against the membrane 70 and typically bonded using heat in a process known to those of skill in the art . between the membrane 70 and the electrode support layer 60 , a layer of carbon 62 may optionally be added . the electrode support layer 60 and , if added , the carbon layer , are often referred to as a gas diffusion layer . in addition , a catalyst layer 64 is provided , which may contain teflon ® ( made by e . i . dupont de nemours and company ) as a binder material . in accordance with the present invention , the catalyst layer 64 includes a catalyst and an additive ( or additives ) in addition to the binder material . as representative examples , the materials forming these layers include a carbon - based material for the electrode support layer 60 , phosphoric acid infused high temperature proton exchange membrane 70 , and a mixture of platinum catalyst and additive ( s ) for the catalyst layer 64 . however , as further described herein , and as would be understood by those of skill in the art , the specific materials used for each layer of the mea 10 can vary depending on preferences and desired characteristics of the resulting mea 10 . as such , the present invention is by no means limited to these specific materials described in the representative example . more specifically with regard to the additive material ( s ), the additive material ( s ) creates a more reactive interface with the pt or pt - alloy catalyst for faster oxygen reduction kinetics because of one or more of the following effects : ( a ) acid molecules with specific adsorption much lower than that of phosphoric acid will leave more reaction sites active for oxygen reduction ( phosphoric acid adsorbs strongly and blocks most of the reaction sites on pt or pt - alloy catalyst particles ); ( b ) presence of fluorinated polymers , ionomers , and acids in the immediate vicinity of the catalyst sites enhances oxygen concentration locally to accelerate its reaction rate at the interface ; and ( c ) optimal wetting property of the additive material ( s ) increases the interfacial area for oxygen reduction reaction provided flooding of the interface due to excess wetting is avoided . the additive material ( s ) can include material ( s ) with desired reactionary properties with the catalytic interface in contact with the acid found in the mea ( conventionally , phosphoric acid ) which can he solid or liquid but must be stable at the desired fuel cell operating temperatures ( e . g ., between about 120 ° c . and 200 ° c .). fig3 is a diagrammatic illustration representing the conceptual implementation of the above - described chemistry , in accordance with aspects of the present invention . as illustrated , layer a is the electrode support layer 60 , layer b ( b 1 , b 2 ) is the catalyst layer 64 , and layer c is the pem membrane 70 . the magnified portion of the catalyst layer 64 ( layer b ( b 1 , b 2 )) shows a catalyst support particle o , a catalyst particle p , and an additive material particle q . the catalyst support particle o can be , for example , a high surface area carbon / graphite powder . the catalyst particle p can be , for example , a platinum or platinum alloy . the additive material particle q can be , for example , one or more of the additive materials described herein . in the electro - chemical process relied upon by the present invention , the following reactions occur at the interface shown in fig3 . as shown above , a total cell reaction ( 3 ) represents a cell reaction in an operating h2 / o 2 ( air ) fuel cell while individual electrode reactions at the anode and the cathode are described in an anode reaction ( 1 ) and a cathode reaction ( 2 ), respectively . the anode reaction ( 1 ) takes place at the interface of the anode - pem interface ( b 1 - c in fig3 ), where the h 2 molecules dissociate to produce protons and electrons . when the anode and the cathode are electrically connected , the electrons flow through the external circuit , while the protons migrate to the cathode through ionic conduction . the o 2 molecules ( in air ) fed at the cathode meet the migrated protons and electrons at the interface of the cathode - pem interface ( c - b 2 in fig3 ), where the cathode reaction ( 2 ) takes place producing h 2 o molecules . in accordance with the present invention , it should be noted that the anode reaction rate is faster than the cathode reaction by orders of magnitude . for example , at a practical operating voltage ( o . 67 v / cell ) of ht pem fuel cell , the overvoltage ( voltage loss : theoretical voltage minus the actual operating voltage ) at the anode is typically & lt ; 20 mv ; whereas the cathode overvoltage can be & gt ; 400 mv . it is established that most of this overvoltage is activation overvoltage , which means the voltage loss is due to the very slow rate of the cathode reaction . accordingly , the present invention modifies the cathode - pem interface to enhance the rate of oxygen reduction reaction ( orr ) represented in the cathode reaction ( 2 ). this interface is further illustrated in the magnified portion of fig3 , where the reaction site ( r ) is located at the three - phase ( catalyst - electrolyte - oxygen ) interface , the electrolyte phase being the phosphoric acid - infused ht pem . while intimate contact between the catalyst and the ht pem is essential for the creation of the reactive interface ( r ) at their immediate contact area , extension of such reactive surface area in the depth of the catalyst layer necessitates penetration of the electrolyte phase into the catalyst structure , but without blocking the access of oxygen ( air ) to the reaction site ( r ). the optimal wetting characteristic of the catalyst layer with phosphoric acid is thus a critical requirement for optimal operation in accordance with the present invention . as previously stated , conventional ht pem materials have concentrated ( 85 %- 100 %) phosphoric acid infused in a polymer matrix . therefore , the cathode - pem interface ( c - b 2 in fig3 ) in a ht pem mea essentially contains catalyst ( supported or unsupported pt or pt - alloy ) particles on the electrode side ( b ( b 1 . b 2 )) and phosphoric acid on the electrolyte side ( c ). a phosphoric acid molecule in equilibrium with its successively dissociated anionic species is shown in fig3 and reaction scheme 1 herein . strong adsorption of these species and low solubility of oxygen in phosphoric acid are considered contributing significant factors for the slow rate of orr at the pt - phosphoric acid interface . the addition of trifluoromethanesulfonic acid in 85 % phosphoric acid results in significant enhancement of the orr rates in the mixed acid of different composition ( e . g ., enayetullah at al ., j . applied electrochem , 18 , 763 , 1988 . ); the additive acid , in addition to being weakly adsorbing on the pt surface , has much a higher solubility of oxygen within . in accordance with the present invention , judicious selection of additive materials to the catalyst layer is based on their weaker adsorption ( on pt ) and higher oxygen solubility as compared to those in concentrated phosphoric acid . the wetting characteristic of the additive by phosphoric acid is another factor that can affect the orr rate , more the wetability of the catalyst layer favors the creation of a larger interfacial area . however , excessive wetting of the catalyst layer causes a flooding situation , preventing access of oxygen molecules ( from air ) to the reaction site . the addition of teflon particles as a non - wetting agent in the catalyst phase is necessary to minimize flooding of the interface . the present invention creates an optimal interfacial structure with the additive acidic materials ( with high oxygen solubility and week specific adsorption ) in immediate contact with the catalyst particles ( reaction sites ( r )) and the phosphoric acid , optimally wetting the additive / catalyst surface for enlarged reactive interfacial area . in accordance with the present invention , high performance meas for high temperature pem fuel cells operating at temperatures between about 120 ° c . and 200 ° c . include concentrated phosphoric acid infused in a high temperature polymer matrix . the pem - electrode interface structure is altered to include an additive material ( or materials ) together with a catalyst . the catalyst layer is typically fine particles of platinum ( pt ), or the pt particles supported on high surface area support materials . in accordance with the present invention , the catalyst layer is modified by inclusion of the additive material ( s ). the additive material ( s ) can be in solid or liquid form , and be a particle ( or particles ) having desired reactionary properties with the acid in the ht pem , and which is stable at temperatures of ht pem fuel cell operation ( e . g ., 120 ° c . to 200 ° c .). illustrative examples of such additive materials include , but are not limited to : fluoropolymers : perfluoro ionomers , e . g ., nafion ® and other equivalents phosphates : zr 3 ( p0 4 ) 4 , zr ( hp0 4 ) 2 , hzr 2 ( p0 4 ) 3 , ti ( hp0 4 ) 2 , kh 2 p0 4 , csh 2 p0 4 , mghp0 4 , hsbp20s , hsb3p20s , hssbsp202o , etc . sulfates : ivihso4 ( m : li , na , k , rb , cs & amp ; nh 4 ) polyacids : h3pw1204o . nh20 ( n = 21 - 29 ), h3siw1204o . nh20 ( n = 21 - 29 ), hxw03 , hsbw06 , hnb03 , htinbos , hsti409 , hsb03 , h2mo04 , etc . selenites and arsenites : m3h ( se04 ) 2 ( m : cs , rb and nh4 ), kh2as04 , u02as04 , etc . phosphides : zrp , tip , hfp , etc . oxides : ah03 , sb20s , sn02 , zr02 , etc . silicates : zeolites , h - natrolites , ii - mordenitcs , clays , etc . superacids : sb2fs , fluorosulfonic acids , sulfonic acids , etc . the additive material ( s ) can be a nano - structural material of an organic or inorganic acid , or acid salt with suitable wetting property in contact with phosphoric acid , some examples of which are included above , and others of which would be understood and identifiable by those of skill in the art , as such the above list is in no way limiting to the materials available for use in accordance with the present invention . the amount of the additive material in the catalyst layer is in the range of 1 to 15 % of the catalyst weight . with the inclusion of the additive ( s ), in accordance with the present invention , the resulting high temperature pem meas have a power density per unit area of , for example , 180 - 300 mw / cm 2 at 0 . 67v with ambient pressure h 2 / air operating at 180 ° c ., as compared with a conventional ht pem mea having a power density per unit area of 120 - 150 mw / cm 2 at 0 . 67v with ambient pressure 1 h / air operating at 180 ° c . numerous modifications and alternative embodiments of the present invention will be apparent to those skilled in the art in view of the foregoing description . accordingly , this description is to be construed as illustrative only and is for the purpose of teaching those skilled in the art the best mode for carrying out the present invention . details of the structure may vary substantially without departing from the spirit of the present invention , and exclusive use of all modifications that come within the scope of the appended claims is reserved . it is intended that the present invention be limited only to the extent required by the appended claims and the applicable rules of law . it is also to be understood that the following claims are to cover all generic and specific features of the invention described herein , and all statements of the scope of the invention which , as a matter of language , might be said to fall therebetween .