referring to fig1 a schematic diagram of a typical circulating , bipolar zinc - bromine system is shown . this system can benefit from the inventive method of construction which will be hereinafter described with reference to fig2 through 7 . the zinc - bromine system of fig1 comprises two electrolytes which are circulated through separate compartments 8 , 9 respectively , of the cell 10 . an anolyte which is generally stored in reservoir 11 is pumped via pump 12 through compartment 8 and loop 13 , generally referred to as the anode loop . a catholyte which is generally stored in reservoir 14 , is pumped via pump 15 through compartment 9 and loop 16 , generally referred to as the cathode loop . the zinc - bromine system is also a two phase system , in that the catholyte has bromine complexing agents and is comprised of a first aqueous phase and a second , non - aqueous , bromine - rich phase . the bromine - rich ( complexed ) phase tends to separate at the bromine active electrode 17 from the aqueous catholyte . this non - aqueous phase is stored in the reservoir 14 , as illustrated schematically by shaded portion 14a . a separator 18 delinates and defines the boundary between the anolyte and cathode compartments 8 and 9 , respectively . the separator 18 is a membrane which prevents or binders movement of anions such as the bromide and tribromide ions from cathode compartment 9 to the anode compartment 8 . in a bipolar design , the zinc active electrode 19 and the bromine active electrode 17 are opposite sides of the same electrode structure . further description of the zinc - bromine system can be obtained with reference to aforementioned u . s . pat . no . 4 , 105 , 829 ; issued aug . 8 , 1978 . the zinc - bromine system can be made more practicable by integrating and improving various components of fig1 as will be hereinafter explained with respect to the inventive construction shown in fig2 through 7 . where applicable within the description , like components may have similar numerical designations for the sake of brevity . now referring to fig2 an improved electrochemical system is shown in a schematic perspective view . the improved system utilizes an integrated two - leaved separator - spacer and electrode forming a portion of a stack of cells , as depicted in the exploded view of fig3 . the electrochemical system of fig2 comprises a battery stack 25 which in turn is comprised of a plurality of cells 10 , each having two plates , as shown in fig3 . one plate , according to the invention , is an integral separator - spacer 28 and the other plate is an electrode sheet 29 . the separator - spacer has two functions combined in a single sheet . the first purpose is that of the separator 18 in fig1 i . e . to provide fluid communication between compartments as a membrane . a more detailed description of this function can be obtained from the above - mentioned u . s . pat . no . 4 , 105 , 829 ; issued aug . 8 , 1978 ; and also from u . s . pat . no . 4 , 259 , 417 ; issued mar . 31 , 1981 for an &# 34 ; ionic barrier &# 34 ;, to inventors : r . j . bellows and p . g . grimes . the second function of sheet 28 is to space the sheet 28 from the adjacent electrode sheets 29 so as to create respective anolyte and catholyte compartments 8 and 9 ( fig1 ). the separator - spacer sheet 28 has a microporous mid - portion surface 30 which is recessed from the non - porous surface 31 of the sides , as shown in more detail in fig6 and 6a . when the separator - spacer sheets 28 are pressed between electrode sheets 29 , the stack structure 25 is formed , as shown in fig2 . the projections 32 on the microporous mid - portion surfaces are designed to maintain a spaced compartmental distance between the separator - spacer surface 30 and the flat conductive surfaces 33 of adjacent electrode sheet 29 . the projections 32 provide structural means against collapse of surfaces 33 upon surfaces 30 and vice versa . the projections 32 on one side 30 of sheet 28 are diametrically opposite corresponding projections 32 on the opposite side 30 of sheet 28 as clearly illustrated in fig6 a . this is done , to provide a greater strength against distortion of surfaces 33 upon surfaces 30 . the projections 32 usually are designed as pebbles as depicted by arrows 32a in fig6 a , and as also shown in fig7 cc and 7dd , etc . these projections 32 may also be designed with a rod - shape as depicted in fig7 a , 7aa and 7b , 7bb ; by arrows 32b . the projections 32 may also be a combination of pebble and rod - shaped protuberances as depicted in fig7 c , 7cc and 7d , 7dd . the design of these projections allow for an expeditious flow of electrolyte through the compartments 8 and 9 , respectively . the flow of electrolyte is accomplished without entrapping gas bubbles about projections 32 within the compartmental cavities 8 and 9 . the mid - portion of the separator - spacer sheet 28 can be comprised of a microporous membrane material known as daramic ®, series hw - 0835 , which is made by w . r . grace co ., polyfibron division , cambridge , mass . the raised side borders 31 of non - porous material may be any moldable plastic . the plastic of borders 31 is typycally overmolded around the separator - spacer insert by injection molding , as can be seen from fig6 a . sheets 28 and 29 are assembled by means of hollow male / female connectors 40 shown in detail in fig6 and 6a . when the sheets 28 and 29 are assembled in a stack 25 , these hollow connectors 40 form electrolyte manifolds which supply compartments 8 and 9 with electrolyte via individual conduits or channels 60 . the male / female connectors 40 of sheets 28 fit through the holes 41 ( fig4 and 4a ) in adjacent sheets 29 , and snap into mating connectors 40 in subsequently adjacent sheets 28 . the electrode sheet 29 of fig4 and 4a is comprised of a coextruded sheet of plastic which has an electrically conductive mid - portion 33 and two side portions 37 of electrically non - conductive ( insulating ) plastic . the top and bottom side portions 37 are coextruded &# 34 ; side - by - side &# 34 ; along with the mid - portion 33 to form a one piece continuous electrode sheet , which continuous sheet is then cut to specific lengths to form a plurality of smaller sheets 29 . the edges 38 of sheet 29 may be undercut to improve electrical isolation in stack 25 . this &# 34 ; side - by - side &# 34 ; profile co - extrusion of insulating and conductive plastic sheets 37 and 33 , respectively , presents a new and an alternative fast method of production for all monopolar and bipolar electrodes including electrodes for zinc bromine batteries . compared with compression molding , the co - extrusion method gives more uniformity in thickness , a stronger bonding between the insulating and conductive plastics , much desired flatness , and &# 34 ; electrode by yards &# 34 ; similar to dress fabrice . the fabrication cost is much lower because the process is continuous . a special formulation of carbon plastic is needed for mid - portion 33 of sheet 29 to provide good electrical conductivity , which still exhibit good extrudibility , good strength , and excellent anticorrosive properties against bromine and zinc bromide in the electrolyte . the preferred composition of the conductive carbon plastic is covered by aforementioned u . s . pat . no . 4 , 169 , 816 ; issued oct . 2 , 1979 , to h . c . tsien . this formulation gives good conductivity ( 1 to 2 ohm - cm in resistivity ), good flex strength , low permeability inertness to bromine , good extrudibility , better weldability and less mold shrinkage . the conductive plastic is a mixture of 100 parts by weight of polyolefin copolymer , 25 parts by weight of special conductive carbon , 5 parts by weight each of carbon fiber and glass fiber , and 1 part by weight of fumed silica powder . some of the other advantages of co - extruding the section 33 and 37 are : 2 . maintaining width , flatness and thickness dimensions with the tolerances specified . fig5 a , 5b and 5c are respective top , front and side views of an extrusion die used to fabricate the electrode sheet . the center extrusion die 47 receives conductive plastic from a horizontal extruder through conduit 46 , while the side extrusion dies 48 , each receive non - conducting plastic from an overhead , vertical extruder via conduits 45a and 45b , respectively . the horizontal extruder for the black conductive plastic is a 21 / 2 &# 34 ; screw with l / d of 30 : 1 , while the vertical extruder for the opaque insulating plastic is a 11 / 2 &# 34 ; dia . screw with l / d of 24 : 1 . the melted insulating plastic enters into the die at 90 degrees from the vertical stream 45 , divides into two steams 45a and 45b and flows into one left and one right separate &# 34 ; coat hangers &# 34 ; along side the main coat hanger 45 . the die design is conventional , except that the side - by - side profile division is believed to be novel . the die is of split construction in order to facilitate any changes in the design and the ease of fabrication . the main die assembly consists of a lower die body 55 , upper die body 56 , flexible upper lip 57 and fixed lower lip 58 . the die lip gap is ground to allow for the swell of plastics emerging out of the die . lip gaps can be individually adjusted by screws 59 in conjunction with the nut bars 61 . the two side plastics 62 and 63 close the two outsides of flow channels of the insulating plastics and give a box - like reinforcement . adapter 64 provides connection to the main extruder . there are ( 16 ) cartridge heaters 65 and ( 4 ) band heaters 66 for heating the two streams of plastics . temperatures are controlled through thermocouples and individual zone temperature controllers . the individual adjustment of the left and right streams 45a and 45b is made possible by ball headed adjusting screws 67 and locknut 68 . bushings 74 make good connection from valve blocks 75 to die block 56 . all main parts of the die are made of a2 air hardening tool steel . the bethelehem a2 air hardening steel has the following physical properties : ______________________________________ as - annealed heat treated______________________________________hardness ( r / c ) 15 - 20 56 - 58yield strength psi 55 , 000 208 , 750u . t . s . psi 114 , 950 255 , 250elongation % 18 % . 8 % ______________________________________ with the head pressures from the extruders well over 1000 psi , the die cannot operate free from internal leakage between the insulating and conducting streams if the die is in the soft annealed condition . the hardened and reground die eliminates internal leakage . four different types of insulating plastics were tried , they are : ______________________________________ melt flow index______________________________________fiberfil j60 / 20e 230 ° c ., 2160 gm load , 4 . 5 gm in 10 min . ugi lr711 hdpe 190 ° c ., 2160 gm load , 10 . 5 gm in 10 min . exxon p . p . 5052 p . p . 230 ° c ., 2160 gm load , . 9 to 1 . 5 gm in 10 min . exxon p . p . 5011 p . p . 230 ° c ., 2160 gm load , . 45 to . 85 gm in 10 min . ______________________________________ both exxon homopolymer pp5011 and 5052 can match well with the conductive plastic . they came out of the die with no wrinkles , the sheets were flat and uniform . theoretically , aside from previous considerations , any polyethylene or polypropylene for side portions 37 can be a good match with the conductive plastic mid - portion 33 , because the basic material used in the conductive plastic is the copolymer of the two . the melting points are in the range of 325 ° to 375 ° f . therefore , approximately 400 ° f . is a proper temperature in range for the two streams to meet . head pressures are 1500 to 1800 psi . these conditions made a good bond at the bonding line . close match of melt indices is necessary in order to eliminate scallops formed at the joint of the two edges . the viscosities and velocities of the streams from the two extruders has to be very closely equal . pressures can be manipulated from two heads while varying the temperatures in various die zones to get the matching conditions . however , the differences between melt flow index of conductive and that of insulating plastics has to be minimized . the extrusion speed can be around 20 ft ./ minute to 90 ft ./ minute . there are many downstream attachments that can be added so that the co - extruded sheet can be worked on while still hot and soft . thus , the repeated heating and cooling cycles with the accompanied plastic degradations can be eliminated . powder of activated carbon can be sprayed on one face of the carbon plastic as the sheet is emerging from the die and before the sheet is pinched by the cold nip rolls . the powder spray is limited in the conductive area . various types of surface finishes can be obtained by changing the nip rolls from polished chrome - plated surfaces to teflon coated and rubber rolls . it is also possible to replace nip rolls with dimpling rolls , so that cavities or special flow patterns can be formed on one or both faces of the co - extruded sheet . the hot forming rolls can make repeated patterns of design indentations in the electrode , if so desired . the combination possibilities are only limited by imagination . for dimpling , the design is also repeated every revolution of the dimpling rolls . it is very much like printing repeated patterns on the fabric . these downstream modifications such as catalyst spraying , dimpling , or hot forming can be added so that all operations can be done without significant added production cost . fig5 is a schematic perspective view of the continuous electrode sheet emerging from the split die illustrated in fig5 a , 5b and 5c . now referring to fig2 a further safety feature for the electrochemical system is illustrated . in order to prevent or reduce the risk of spilling corrosive bromine and bromine compounds in the event of casing or compartmental rupture , the various compartments can be nested with the bromine - containing compartment 50 being the most internal compartment . the bromine compartment 50 is surrounded by the catholyte - containing compartment 51 , which in turn is surrounded by the anolyte - containing compartment 52 . compartments 50 , 51 , and 52 are all enclosed by outer casing 53 . shunt currents can be eliminated along formed manifolds ( connectors 40 ) by means of applying a protective current along these electrolyte carrying conduits , in accordance with the teachings expressed in aforementioned u . s . pat . no . 4 , 197 , 169 issued apr . 8 , 1980 to m . zahn , p . g . grimes and r . j . bellows . the two - leaved electrochemical cell construction of this invention reduces parts and is easier to fabricate and assemble than prior systems of this kind . further modifications to the invention may occur to those skilled practitioners of this art . such modifications have not been described for the sake of brevity . the scope and breadth of the invention is meant to be encompassed by the following appended claims .