referring now in detail to the drawings , the illustration of fig1 shows schematically a triple hot runner system s which accommodates three thermoplastic resins suitable for use where each has different optimum processing temperatures . one resin is provided from a source identified as extruder a , a second resin is provided from a source labeled extruder b , and a third resin is provided from a source labeled extruder c . while the present exemplary embodiment of the invention discloses three resin sources , it is entirely within the spirit and scope of the invention to utilize more than three resin sources . the portion of the hot runner system leading from extruder a is shown in solid lines , that portion of the system originating with extruder b is shown in dashed lines , and that portion of the system originating with extruder c is shown in dotted lines . in the embodiment of fig1 the sequence of injection is a first injection from extruder a of virgin pet to form the exterior surface of the article , a second injection from extruder b of the evoh barrier resin , and a third injection from extruder c of the filler resin which may be reground pet or any other desired filler resin as polyethylene or polypropylene . if desired one could have a fourth injection of virgin pet to finish the gate area . thus it can be seen that three ( 3 ) separate lines are provided , each with their own temperature control to the nozzle and two separately controlled in the nozzle . where virgin pet and reground pet are used together with evoh , the lack of three separate temperature control systems in the nozzle is obviously not relevant ; however , it has been found that even where a completely different third material is used for the filler excellent results are obtained due to the provision of three ( 3 ) separate temperature control systems to the nozzle . for purposes of convenient explanation of the invention , the portion of the hot runner system connected to extruder a ( solid lines ) for virgin pet is maintained by suitable heaters in well - known fashion at a temperature ranging from 500 ° to 550 ° f ., the optimum processing temperature for a thermoplastic resin such as pet . the portion of the system connected to extruder b ( dashed lines ) for evoh is maintained at a temperature ranging from 400 ° to 440 ° f ., the optimum processing temperature for a thermoplastic resin such as evoh . if the filler plastic is low density polyethylene , the portion of the system connected to extruder c is maintained at a temperature ranging from 350 ° to 400 ° f ., whereas , if the filler plastic is reground pet , the portion of the system connected to extruder c is maintained at a temperature ranging from 480 ° to 550 ° f . it is to be noted that the resin selected and their optimum processing temperatures are merely exemplary of the present invention and their use in the present description is not intended to limit the invention to those specific resins described above . referring further to fig1 the reference numerals 11 , 12 and 13 and 14 designate four mold cavities each communicating with individual nozzles 16 , 17 , 18 and 19 . extruder a supplies a heated manifold m a with for example virgin pet which , in turn , communicates with each nozzle via hot runners or channels 21 , 22 , 23 and 24 , respectively . the reference numerals 26 , 27 , 28 and 29 designate spool valves which operate to control charging of shooting pots or injection cylinders 31 , 32 , 33 and 34 . correspondingly , hot manifold m b supplies for example evoh leading from extruder b to each nozzle 16 , 17 , 18 and 19 via hot runners or channels 36 , 37 , 38 and 39 . spool valves 41 , 42 , 43 and 44 control charging of shooting pots 46 , 47 , 48 and 49 . hot manifold m c , supplying for example reground pet , polyethylene , or polypropylene , leads from extruder c directly to each nozzle 16 , 17 , 18 , 19 via hot runners 50 , 51 , 52 and 53 . it is noted that extruder c leads directly to the nozzles without the use of shooting pots , although shooting pots could of course be used . while the schematic of fig1 shows a hot runner system leading from three sources ( extruders a , b and c ) transporting conditioned thermoplastic resins to a four cavity mold , it is entirely within the scope and capability of the present invention to service as many as 16 to 72 cavities with resins originating from three or more sources . fig2 is a section of the hot runner system in the immediate vicinity of any one of the four nozzle - cavity assemblies of fig1 i . e . cavity 11 and nozzle 16 , for example and is described in connection with an exemplificative embodiment . a central manifold block 61 maintained at an operating temperature ranging from 500 ° to 550 ° f . for virgin pet by heating elements 62 - 62 receives plasticized resin from extruder a through channels 63 and 64 . spool valve or rotary valve 66 , in circuit with channel 64 and operated ( rotated ) by link mechanism 67 , controls the charging of reservoir 68 of the shooting pot or injection cylinder 69 equipped with an injection piston or charging piston 71 . the spool valve 66 is formed with a transverse throughbore 72 and is shown in fig2 in the closed position . the reservoir 68 communicates with channel 73 which leads to the nozzle assembly indicated generally by the reference number 74 . heating elements 62 - 62 maintain the desired processing temperature of channel 73 . heat conducted from manifold block 93 to a central portion of the nozzle assembly 74 maintains the integrity of the desired temperature range within the nozzle in a manner which will be described in more detail hereinafter . a manifold segment 75 secured to manifold block 93 is heated by elements 76 - 76 to maintain optimum temperature of to 440 ° f . for evoh in the hot runner connecting extruder b ( not shown in fig2 ) to channel 77 leading to the reservoir 78 of a second shooting pot 79 equipped with an injection or charging piston 81 . here again , a spool valve 82 ( shown in fig2 in the closed position relative to channel 77 ) controls charging of the reservoir 78 . in the closed position of the spool valve 82 , the reservoir 78 communicates with the nozzle assembly 74 via channel 80 by virtue of cut - out 85 . when the spool valve 82 is open the channel 80 is closed . link mechanism 90 operates to rotate valve 82 . referring to fig3 note that the nozzle assembly 74 includes a central spigot 83 in thermal contact with manifold block 93 immediately adjacent local heating elements 95 - 95 as is most apparent in fig2 . the spigot 83 , fabricated preferably of a good metallic thermal conductor such as beryllium copper , is formed with through channels 84 and 84a through which flow material from extruders a and c to the nozzle gate 86 . the spigot is supported by minimal bearing surfaces 87 - 88 in a housing 89 which is spaced from the spigot substantially throughout its length by an insulating air gap 91 . this air gap blocks conduction of heat from the spigot 83 to the housing 89 to preserve maintenance of the evoh at its optimum process temperature controlled by heating means 192 as evoh progresses through channel 90 of the housing to gate 86 . extruder c transfers material via channel 92 in manifold block 93 directly to nozzle channel 84a in spigot portion 83 . manifold 93 is insulated from manifold 61 by space 94 and has its temperature controlled separately therefrom by heaters 95 - 95 . this enables independent temperature control of the resin from extruder c all the way to the nozzle . thus , it is apparent that the hot runner system of the present invention is effective to maintain different optimum process temperatures appropriate to two different resins from the source of the resin to a nozzle gate , and a third resin from the source of the resin to the nozzle . to prime the hot runner system initially , extruders a and b including their cooperating shooting pots 69 and 79 are purged . extruders a and b are moved into operative position relative to their respective manifolds . with valve stem 100 and spool valves 66 and 82 in the open position shooting pot reservoirs 68 and 78 are charged with for example virgin pet and evoh compound , respectively . next valve stem 100 is closed and purged resin in the mold cavity is removed . thereafter the mold is closed and clamped , valve stem 100 is opened and an automatic sequence occurs as follows : spool valve 66 is closed and injection piston 71 is advanced until it bottoms at the point indicated by the reference numeral 101 discharging a measured amount of virgin pet into the mold cavity through channel 73 and gate 86 . this constitutes the first shot of virgin pet into the mold cavity as shown schematically at f in fig4 . the piston 71 is held forward ( in its bottomed position 101 ) blocking access to reservoir 68 to prevent backflow of virgin pet compound from channel 73 into reservoir 68 . that is , the piston 71 is held bottomed to block access to reservoir 68 because upon subsequent operation of piston 81 to inject evoh , the evoh injection pressure has a tendency to displace virgin pet from channel 73 back into reservoir 68 . nest spool valve 82 is closed to extruder b and opened to channel 80 . operation of injection piston 81 until it bottoms at 102 discharges a measured amount of evoh into the cavity through channel 80 and gate 86 . this constitutes the shot of evoh into the mold cavity ( second shot of resin ) to develop a three ( 3 ) layered wall as shown schematically at s in fig4 . the volume of the first and second shots of resin is less than the total volume of the mold cavity . next channel 80 is closed by appropriate rotation of spool vavle 82 . next extruder c discharges a measured amount of third resin as filler via channel 92 . the third resin can be scrap pet or polypropylene or other suitable material . this step constitutes the third shot of resin to develop a five ( 5 ) layered wall as shown schematically at t in fig4 . thus , a five ( 5 ) layered wall structure is molded using three ( 3 ) resins as shown in fig5 wherein reference numerals 105 and 107 represent the first shot of virgin pet , reference numerals 108 and 109 represent the second shot of evoh , and reference numeral 106 represents the third shot of filler . after packing is completed valve stem 100 is moved to closed position and piston 71 is freed to move . pet extruder a is operated to recharge reservoir 68 of shooting pot 69 displacing piston 71 until it contacts an injection stop sa ( fig2 ). the position of the stop sa controls and measures the amount of pet introduced into the reservoir 68 . in similar fashion the injection stop sb ( fig2 ) controls and measures the amount of evoh introduced into the evoh reservoir 78 . during the course of packing the mold cavity ( the part ) the evoh reservoir 78 is recharged by opening spool valve 82 to allow extruder b to displace evoh piston 81 until the piston contacts its injection stop sb thus charging evoh reservoir 78 with a measured amount of evoh compound . after a suitable cooling interval , the mold is opened and the article is ejected by know means . the above cycle is then repeated to generate additional layered articles or performs in continuous , automatic fashion . it is to be understood that the operation just described occurs simultaneously in all four mold cavities 11 , 12 , 13 and 14 of fig1 or in any number of mold cavities as considerations of mold design and production requirements dictate . it is to be understood further that the invention is not limited to the illustrations described and shown herein , which are deemed to be merely illustrative of the best modes of carrying out the invention , and which are susceptible of modification of form , size , arrangement of parts and details of operation . the invention rather is intended to encompass all such modifications which are within its spirit and scope as defined by the claims .