fig1 illustrates the extreme constructive complexity of a fuel cell stack according to prior art . as fig1 shows , each individual cell of a hydrogen / oxygen fuel cell stack generally requires a bipolar plate a , a hydrogen gas distributor ring b , an ion exchange membrane c , coated with catalyst , an oxygen gas distributor ring d , seal rings e for sealing these components , and the current distributor structures f . these are in all 10 components per individual cell . if for example a stack output voltage of 70 volts is to be produced , in the case of an individual cell voltage of 0 . 7 volts , 100 individual cells are required , i . e . 1 , 000 components must be combined , and 400 seal rings fixed . fig2 a shows the regions , disposed one behind the other , of a strip membrane , with insulating regions 2 , 4 . the first region 1 in this case is purely ionically conductive , and shows the membrane surface of the individual cell . the second region 2 is both ionically and electronically non - conductive and represents the insulating region . the third region 3 is purely electronically conductive , and the fourth region in turn is both ionically and electronically nonconductive and in turn represents an insulating region . these units are now periodically repeated in a strip membrane . the sequence of regions 1 to 4 shown in fig2 a is symbolised in illustrations 2c and 5 by the rectangle 7 . the units 1 to 4 form a membrane unit and represent the basic unit of the finished strip membrane ( shown without series incorporation for reasons of improved clarity ). fig2 b shows a cross - section through such a membrane . in this case the strip membrane is of a thickness varying in a region between 0 . 5 μm and 1 μm , preferably in a region between 10 μm to 200 μm . all surfaces from which the strip membrane is built up accordingly likewise have thicknesses in this order of magnitude . the surfaces of the respective regions depend on requirements , i . e . on the power which is to be produced by the strip membrane . the surface areas of each individual region in this case can come to 1 mm 2 to 1 , 000 , 000 mm 2 . fig3 now shows the in - series incorporation of a strip membrane as described in fig2 . an essential feature of the invention here is that the lower electrode surface 10 of a first individual 6 is connected in series via the electronically conductive region 3 with the upper electrode surface ( 10 ) of a second individual cell 12 . as , in the embodiment according to fig3 insulating regions 2 , 4 are provided , the in - series incorporation must be effected by an additional coating 11 . the periodic repetition of such units shown in cross - section in fig3 then forms a strip membrane . thus the strip membrane 5 may be produced from separate , finished individual surfaces . in this case all the individual surfaces required to build up the strip membrane ( i . e . the individual regions of the respectively used type of membrane , and if necessary separating regions and lateral strips ) are separately produced before manufacture of the actual membrane in the required size , and subsequently connected to provide the overall strip membrane 5 . films of the corresponding materials are used ( polymeric films , films of modified polymers , etc .) from which pieces of the required shape are cut . the ionically conductive regions 1 of the membrane may be already coated with electrode material 10 , or coating with electrode material 10 may be effected after combination of the individual pieces . the pieces are disposed in the geometrical configuration of the strip membrane type to be manufactured , and are connected together in a permanent and gas - tight manner . the pieces are connected by previously known adhesive methods such for example as adhesion by solvents , dispersions , melting agents , contact or reaction adhesives , or by thermal methods such for example as welding , so that a surface results consisting of one piece , which permits no direct gas contact between the upper and lower sides of the membrane . in reinforcement of this , the individual surfaces may be connected by additional compression . another possible way of manufacturing membranes consists in using polymeric materials which may be changed into the free - flowing condition , i . e . which are for example meltable or soluble in specific solvents . all the regions of the membrane are produced in that the free - flowing materials are applied by suitable metering and distributing devices to a substrate ( such for example as a glass plate ), and films of this material are produced by cooling of the melt or evaporation of the solvent . this application of the various regions may be done in succession , i . e . the first material is applied in a free - flowing form to the substrate and cooled ( melt ) or dried ( solution ), so that a film results on the substrate . then the next material of the adjacent region is applied in a free - flowing form and the film is produced . in the selection of suitable materials which are compatible with one another , it is possible that , by means of the respective application of the free - flowing material , the lateral regions of the adjacent region already produced , will be dissolved as well in the case of dissolved materials and , in the case of molten materials , may be transferred into the plastic state ( polymers ), so that a bond with the adjacent region results simultaneously with the application of the respective free - flowing material . subsequent adhesion / welding of the regions , even under pressure , is possible . in another possible method , the various regions may be applied simultaneously . for this purpose the materials brought into the free - flowing condition are applied via suitable metering and distributor arrangements simultaneously and next to one another to the substrate in such a way that the various materials , still in a free - flowing state , mix in the lateral regions on the substrate . subsequent drying ( in the case of dissolved materials ) or subsequent cooling ( in the case of melts ) fixes the materials which are already connected together . finally , the membrane is released from the substrate . additional subsequent adhesion / welding of the regions is possible . the simultaneous application of the various materials is particularly suitable for continuous manufacturing processes for strip membranes . the electrode coating 10 is applied to the ionically conductive regions 1 of the membrane units . the principle of function of the strip membrane 5 is independent of the type of electrode application ; the technique of application must however ensure the following : the electrode must be applied to the membrane in such a way that an exchange of materials of the ions to be transported is possible between the ionically conductive membrane regions and the electrodes . the electrode material must have an electronic shunt conductive capacity , in order to enable current take - off . for example , the application of the electrode material 10 , with or without additives , is possible by pressure methods . in this case the electrode material is the initial material , which may be present for example in the form of powder , and is pressed together with the membrane . a possible type of such a method is contained in appleby , yeager , energy ( oxford ), 11 ( 1986 ), 137 . if thermal plastic polymers are used for the ionically conductive regions 1 of the membrane , the electrode material 10 may be particularly well combined by pressure at high temperatures with the regions , as these latter may be transferred into the plastic condition by the heating . if soluble polymers are used for the ionically conductive regions 1 , an intensive electrode bond is achieved by superficial dissolution of the regions with suitable solvents before application of pressure . in this method , the electrode material 10 may be present for example as a powder , or in the form of a film ( e . g . be applied on to a carrier or polymer - bonded ) or as a solid block of material . another possibility is to apply the electrode material 10 as a suspension , with or without additives , in the free - flowing condition , to the membrane , and to produce the electrode coating by drying . in this case , when soluble materials are used for the ionic regions of the membrane units , the membrane surface may be dissolved by the suspension , so that after drying the desired internal bond between ionically conductive material and electrode results . it is likewise possible to precipitate the electrodes by thin - layer methods , ( such for example as sputtering or plasma processes ), if necessary with suitable masks , to the membrane ; subsequent treatment of the layers may follow in order to achieve a porous structure . in order to improve the shunt conductive capacity of the electrode layer it is possible to apply to the catalysts layers integrated in the membrane electrically conductive structures for current collection ( e . g . metallic nets ), these being glued , pressed or welded to the membrane . for the preferred embodiment with the insulating regions 2 , 4 , electronically conductive compounds 11 must be applied . these must enable the electrical connection of electronically conductive surfaces , the electronically conductive surfaces involving the electronically conductive electrode layers 10 and the electronically conductive regions 3 of the membrane units . in this case the electrically conductive material 11 used is applied to the membrane between the regions to be connected . the most various methods are possible for applying the electrically conductive material 11 to the membrane . the functional principle of the strip membrane is independent of the type of application ; the technique of application need only ensure the electrical connection of the desired regions . thus for example it is possible to glue films of electrically conductive material 11 with electronically conductive adhesive to the membrane . likewise , the use of thermoplastic polymers may render possible welding of the films to the membrane . adhesion is rendered possible by the use of soluble polymers by means of dissolution procedures of the membrane surface or of the conductive films . furthermore , polymer solutions may be used which contain electrically conductive particles , the suspension being applied to the membrane and , after evaporation of the solvent , the conductive structure results . thermoplastic polymers modified in order to achieve electrical conductivity may also be applied in the molten state to the membrane and be connected therewith . it is likewise possible to precipitate the electrically conductive layers 11 by means of thin - layer methods ( such for example as sputtering or plasma processes ), if necessary with suitable masks , to the membrane . the electronically conductive connections 11 may consist of the same material as the electrodes , and may be applied in the same working step with them to the membrane , e . g . by means of the pressing method described in the application of the electrode material . fig4 now shows the structure and circuit incorporation of a strip membrane in which the electrode surface 10 simultaneously fulfils the role of the electronically conductive regions . the essential factor here is that the upper electrode surface 10 of a first individual cell 13 is directly connected with the lower electrode surface 10 of a second individual cell 14 , and thus undertakes electrical series incorporation of the individual cells . this bond must be electronically conductive and impermeable to gas . in particular , the structure of the strip membrane , in which the electric surface 10 simultaneously fulfils the role of the electronically conductive regions , is built up from separate complete individual cells , the coating of the ionically conductive regions with electrode material being effected before connection of the individual pieces . the adhesion or welding of the individual surfaces must be electronically conductive . fig5 shows now the diagrammatic structure of a one - dimensional strip membrane 5 . the numeral 7 represents the regions 1 to 4 described in fig2 a or 2b . these regions 1 to 4 , identified by 7 - fig2 c are now shown as in fig3 incorporated in series and thus forming the one - dimensional strip membrane 5 . this arrangement is termed a one - dimensional strip membrane and may possess on all four sides lateral strips 8 of electronically non - conductive material . fig5 shows the structure with reference to the example of a one - dimensional strip membrane which consists of four basic units . fig6 shows the arrangement in which two one - dimensional strip membranes 5 are incorporated in parallel . the individual strip membranes in this case are connected together by separating regions 9 of electronically non - conductive material . this arrangement is termed a two - dimensional strip membrane , and may in turn have on all four sides lateral strips 8 of electronically non - conductive material . fig6 shows the structure with reference to the example of a two - dimensional strip membrane consisting of two one - dimensional strip membranes 5 with four respective basic units .