[ 0040 ] fig1 shows the apparatus for the practice of the method , comprising the plasticizing extruder 1 and the plastic - melting extruder 30 . in fig1 to 5 , the plasticizing extruder 1 according to the invention can be seen as a dual screw extruder with a length l . as fig1 shows , the length of the plasticizing extruder 1 is divided into two working areas and configured accordingly , namely into a feed and impregnating section m and an output and transport section n . for the shaping discharge of the product 24 ( a fiber - reinforced plastic composition ) a discharge nozzle 8 is provided at the end . fig2 shows section a - a of fig1 the fiber material 10 in bulk form being drawn into the infeed opening 18 . the plasticizing extruder 1 includes furthermore the housing 25 with the housing bores 2 and 3 as well as the extruder axes 6 and 7 for the feed screw 5 and the tandem screw 4 in the feed and impregnation section m , the housing 26 with the bores 2 ′ and 3 ′ for the extruder screws 4 ′ and 5 ′ of the discharge and transport section n . in fig1 there is shown the plastic melting extruder 30 for the preparation of the plastic from the hopper 19 for the feeding and transfer mechanism 29 , and drive 20 ′. the plastic transfer mechanism 29 passes the prepared plastic film 11 through the plastic introducing funnel 28 and into the discharge nozzle 13 . the drive 20 serves to drive the extruder screws 4 / 5 and 4 ′/ 5 ′. in the manufacturing operation the fiber material 10 is driven by the feed movement into the feed passage 27 and from there toward the product discharge by the screw units of the plasticizing extruder 1 through the screw land 9 and the screw root 22 . the fiber material 10 with the molten plastic is driven by the screw extruder 1 , with its two screws rotating in the same sense , from the feed screw 5 to the tandem screw 4 and vice versa in the discharge direction . that means that the fiber material 10 is driven in a kind of wrap - around , depending on the infeed width b , with more or less of an overlap , in the direction of the discharge nozzle 8 . during this sliding movement the molten plastic film 11 carried with the fiber material is worked into the fiber material and the individual fibers . as it further can be seen from fig1 to 5 , the fiber material 10 is drawn into the feed slot of the feed opening 18 of the plasticizing extruder 1 with its width b parallel to the extruder axes 6 and 7 and approximately tangentially onto the feed screw 5 , with a ¼ to ¾ wrap - around corresponding to wrap - around angle u around the housing bore 3 , which in some cases is eccentric , and has the diameter d plus 2 to 20 millimeters . the application of the fluid plastic film 11 directly onto the inwardly falling fiber material 10 takes place in the feed opening 18 where the fiber material is pressed into the fluid plastic film 11 applied to the feed screw 5 from the dispensing nozzle 13 . within the feed and impregnation section m all sides of the fiber material 10 thus become wetted or impregnated by kneading on the extruder screws 4 and 5 with the fluid plastic film 11 . then the individual fibers of the fiber material 10 , thoroughly impregnated or imbibed are carried from the feed and impregnation section m into the discharge and outfeed section n , the complete fusion coating and fiber distribution taking place in the case of rodlet granules . depending on the thickness of the fiber material and the matching consistency of the molten plastic it may be desirable for the fiber material 10 to be forced into the grooves and onto the lands 23 of the feed screw 5 by means of a stripping edge 12 or stripper bar 21 . in a preferred embodiment , the feeding of the fiber material 10 is achieved by a feed roll 15 disposed in the feed opening 18 , as shown in fig4 although this is not necessary to practice the present invention . in another preferred embodiment , the drawing of the fiber material 10 into the feed opening 18 is likewise improved by conically flaring the feed area . in yet a further improved embodiment , trouble - free guidance of the fiber material 10 in the feed opening 18 is achieved , according to fig5 in providing a removable feed jaw 16 . this aspect also provides for a simplified cleaning process . this feed jaw 16 can be optionally thermally insulated from the housing 25 and , being heated or cooled by means of a bore 17 , is adjustable to a temperature that is slightly below the tackiness temperature of the fiber material . it is furthermore envisioned that equipping the feed jaw 16 with an oscillatory drive will yield advantageous results . additionally , it is envisioned that the diameter reduction d of the feed screw 5 downstream from the feed opening 18 can terminate spirally in the direction of rotation . in another preferred embodiment , feed area 14 may be expanded conically onto the feed screw . in another preferred embodiment , the invention comprises a plastic melting extruder heating apparatus adapted to heat the fiber material in a transport line to the plasticizing extruder . in yet a further embodiment of the present invention , there is a method for the production of fiber - reinforced plastic compositions using a plasticizing extruder in which cold or preheated concentrate rodlets , recyclate chips , bulk fibers or other granular materials as fiber material are drawn through a guiding gate and a preheating device into the infeed opening of the plasticizing extruder , preferably parallel to the extruder axes and approximately tangentially onto an extruder screw and wound drivingly around the extruder screws and drawn into the cylinder bores of the screw cylinders , at the same time the application of a fluid plastic film to the extruder screw lands takes place and the drawing - in / pressing - in of the fiber material into the fluid plastic film , then the fiber material is wetted or imbibed on all sides with the liquid plastic within a drawing - in and impregnation section with the individual fibers on the extruder screws and carried into a output and transport section and discharged as a fiber - reinforced plastic composition ( plasticate ) susceptible of further processing , characterized in that , in a first extruder , the plastic granules are melted to a preferably higher temperature than the necessary plasticate temperature , in the entrance opening of a second extruder the plasticizing extruder , the molten plastic and the fiber material are combined , and within the feed and impregnating section of the plasticizing extruder the fiber material is largely uniformly embedded in the molten plastic and brought completely to the plasticate temperature in the discharge and transport section , the fiber material being preferably preheated before combination to such an extent that it can still be fed without problems , and without sticking , into the infeed opening , and that the fiber material with the plastic fused onto it is fed into a cylinder bore of the feed screw with a wrap - around of ¼ to ¾ from the point of contact with the fiber material , which has a preferably eccentrically disposed diameter d enlarged by 2 to 20 mm . in yet another embodiment of the present invention , there is an apparatus for the production of fiber - reinforced plastic compositions from fiber material and a melted plastic with a plasticizing extruder and a plastic melting extruder heating apparatus heating the fiber material in the transport line to the plasticizing extruder , an impregnating apparatus in the plasticizing extruder for the introduction of the fiber material and for mixing a plasticizing extruder consisting of a housing with two bores and axes of two extruder screws driven in rotation , a feed opening for the introduction of the fiber material into the bores being provided in the housing , for the practice of the methods , characterized in that , as plasticizing extruder ( 1 ), a parallel double screw extruder with preferably mop - up screw elements of great pitch is provided , which has a slot - like feed opening ( 18 ) above a feed screw ( 5 ), while , beginning from the feed opening ( 18 ) and in the range of the feed screw ( 5 ), the cylinder bore of the feed screw ( 5 ) is made with a ¼ to ¾ wrap - around ( u ) of diameter ( d ) enlarged by 2 to 20 mm , preferably eccentric , and a stripper bar ( 12 ) is disposed at the end , and thereafter the housing bore ( 3 ) of the feed screw ( 5 ) is reduced to the screw diameter ( d ). the foregoing description of a preferred embodiment of the invention has been presented for purposes of illustration and description . it is not intended to be exhaustive or to limit the invention to the precise form disclosed , and modifications and variations are possible in light of the above teachings or may be acquired from practice of the invention . the embodiments were chosen and described in order to explain the principles of the invention and its practical application to enable one skilled in the art to utilize the invention in various embodiments and with various modifications as are suited to the particular use contemplated . it is intended that the scope of the invention be defined by the claims appended hereto , and their equivalents . the foreign priority document , here , german patent application no . de 1 00 59 525 . 1 , filed nov . 30 , 2000 , including the specification , the drawings , the claims , and the abstract , is incorporated herein by reference in its entirety . additionally , u . s . patent application , ser . no . ______ ( claiming priority from german patent application no . de 1 00 59 461 . 1 , filed nov . 30 , 2000 ), including the specification , the drawings , the claims and the abstract , is incorporated herein by reference in its entirety .