fig1 , 2 and 9 show an extruded length of a multi - strip formed bumper product 8 comprising an outer facing strip 10 of relatively hard polymer material , and intermediate strip 20 of relatively soft , rubbery or bendable polymer material and an undersurface strip 40 of relatively hard , rigid , shrink resistant polymer material . the outer coat or strip component / layer 10 is bonded during the extrusion process , preferably immediately upon exit from the final extrusion die , to the outer surface of the inner soft or manually bendable layer or strip 20 such that the end product assumes the outward visual appearance of a relatively hard , shiny surface as opposed to the inner layer 20 which cannot be visually seen when mounted on a rail 30 as shown in fig2 . fig2 shows the elongated strip - like product 8 mounted on a rigid , inflexible metal rail 30 by snap fitting of preformed tongues or detents 55 formed on the underside 57 , fig1 , of the core 20 strip / layer onto a complementary receiving set of grooves or detents 59 formed on the outside surface the rail 30 shown in fig2 . as shown in fig3 , the composite material feed for the core 20 is fed directly from the exit barrel 6 of the extruder through a central composite material bore 50 that extends through each of plates 1 - 4 . the polymer feed for the cap coat 10 is fed through an aperture 60 extending from the exit side to the entrance side of plate 4 through plate 4 , the feed then being routed through a bore 70 , fig7 , 8 , 10 on the entrance side of plate 4 such that the cap coat material feed is ultimately routed through plate 4 and out the exit side of bore 70 on the exit side of plate 4 , fig7 , 8 , 10 simultaneously with the extrusion of the feed material for the core 20 being routed through central bore 50 . the polymer feed for the rigid non - shrink strip 40 is initially fed through an aperture 80 extending from the exit side to the entrance side of plate 4 through plate 4 , the feed then being routed through a groove 90 , fig7 , 8 , on the entrance side of plate 4 such that the rigid strip 40 material is ultimately routed through plate 4 and out the exit side of bore 100 on the exit side of plate 4 simultaneously with the extrusion of the feed material for the core 20 being routed through central bore 50 and the feed material for the cap coat 10 being routed through bore 70 . thus all three separate streams of polymer materials comprising the cap coat 10 , core 20 and rigid undersurface strip 40 are simultaneously co - extruded and come into contact with each other in a molten state immediately upon exit from the exit side of plate 4 . once the three co - extruded streams of materials come into contact with each other in the molten state , the materials firmly bond to each other during and upon cooling to form the product shown in fig1 , 2 , 9 . fig3 shows an additional end plate 5 that may be used together with the plates 1 - 4 assembly , the exact configuration and use of plates and equipment to effect the fluid material feed connections to the bores of plates 1 - 4 being a matter of design choice for the skilled artisan . the disclosed embodiment showing the use of four separate plates 1 - 4 is shown for purposes of example only . any number or configuration of extrusion plates that achieve the function of routing of the thermoplastic polymer materials as shown may be used in the process . positioning the exit ends of feed bores 50 , 70 , 80 in close adjacency to each other such that the separate streams of exiting polymer materials contact the surfaces of each other upon exit from the extrusion plates is most preferred so that the separate streams of exiting polymer materials come into contact with each other in a molten state immediately upon exit and thereby adhere to each other upon cooling from the molten state to a stable cooled state . when the separate streams of polymer materials come into contact with each other in the molten state the mating surfaces mix together somewhat at the point of contact and upon cooling to a crystalline state become essentially adhered to each other to form a the unitary product 8 shown in fig1 , 2 , 9 . the separate streams of extruded polymer materials may alternatively be bonded to each other with a bonding material . fig3 , 10 show a solid rod or wire 200 that may be positioned through the end portion of bore 50 in the middle of the detent 55 configuration of the core 20 strip to enable an elongated aperture 25 to be formed within the body of the detent during the extrusion process to impart additional bendability or flexibility to the detent 55 . such additional flexibility imparted to the detent 55 better enables the detent to be manually snap fit around or over the outer surface of the complementary protrusion or detent 59 of the rail 30 onto which the bumper strip 8 is mounted . the snap fitted mounting of detents 55 onto the protrusions 59 firmly holds the bumper 8 on the rail 30 . the core material 20 typically comprises a mixture of polymer materials that have been previously processed and melted in a prior extrusion or injection molding cycle , e . g . a mixture of scrap materials from previous extrusion cycle runs of one or more selected thermoplastic polymer materials such as polyvinyl chloride ( pvc ) where each scrap material contains a different concentration / amount of dye material and / or a different durometer or hardness . the subsequent extrusion processing cycle carried out on previously extruded or molded materials causes the composite material now being melted a second time in the course of an extrusion or molding process to assume a lower durometer than the originally extruded product comprising virgin material and / or a greater rubberiness , flexibility or bendability than the original virgin material . the lower durometer of scrap material may also be a result of the scrap materials containing several different dye and other additives such as plasticizers and the like . as used herein the phrase “ melted for the first time ” or “ first melted ” or the like means that the polymer material has not been previously melted during an extrusion or molding process , it being understood that the starting polymer material may have been previously in a molten form as a result of its having been produced / manufactured in the first instance . the cap coat 10 thermoplastic material selected is preferably virgin polymer material that has not been previously extruded or otherwise melted and typically does not initially contain a dye . the cap coat 10 material upon extrusion has a higher durometer , rigidity and less rubberiness , flexibility and bendability than the core material 20 . one or more dye materials that comprise between about 3 % and about 10 %, e . g . 4 - 7 %, by weight of the cap coat polymer material may be mixed with / added to the thermoplastic starting feed material for the cap coat 10 . the non - shrink strip material 40 is also preferably comprised of a virgin polymer material that has not been previously extruded or otherwise melted . most preferably , the non - shrink strip material is the most rigid of the three polymer materials and is the most resistant to shrinkage particularly in / along the longitudinal direction of the elongated strip - form product 8 . the non - shrink material may comprise the same or substantially the same virgin polymer material as the core 20 material . the rigid strip 40 provides a particular resistance to shrinkage of the core material 20 along the longitudinal or axial length of the elongated extruded strip - like product 8 by virtue of being bonded to the underside of the core 20 strip . such resistance to shrinkage by virtue of the bonding of the non - shrink strip 40 to the core strip component 20 thus obviates the necessity for replacing edge , end or corner pieces that are typically attached to or mounted at the ends of a finished strip product 8 once installed on a rail 30 in an actual shelf , counter or other retail store environment . the polymer material selected for use in comprising the cap coat 10 and the core 20 typically comprises the similar basic polymers , mixture of polymers or thermoplastic materials , e . g . thermoplastic polyvinyl chlorides , nylons , polyesters , polyethers , polyamides , rubbers and latex rubber materials and copolymers of one or more of all of the foregoing . that is the polymer materials of which the cap coat 10 and the core 20 are comprised typically have essentially the same units making up the polymer backbone . the polymer material of the cap coat 10 and core 20 materials typically differ somewhat in polymer chain length , degree of cross polymerization ( if any ) or in concentration and composition of dye materials contained within the matrix of the materials . for example , the virgin cap coat 10 material typically comprises a polymer material having a durometer of between about 75 and 90 , e . g . 80 - 85 , and the core layer 20 material comprises a mixture of two or more scrap materials that were originally extruded from the same basic material as the cap coat 10 material containing the same or different dye materials at the same or different concentrations as the cap coat 10 material contains . polymer materials suitable for use in the invention are thermoplastic polymers that are relatively pliable or manually bendable such as polyvinyl chloride , polyamide , polyether , polyester and copolymers of all of the foregoing with one or more of each other or with urethane or other polymer units that impart a suitable manual bendability to the end polymer . stiffeners , plasticizers , catalysts and the like may be contained within the polymer materials to impart any desired degree of flexural modulus , hardness , impact resistance and like mechanical / physical properties to the polymer material .