Abstract: The specification discloses a heated extruder nozzle for extruding semi-fluid material such as ground meats and other food products. The nozzle includes a chamber having a baffle wall dividing the chamber into a first and second baffle area with these baffle areas in fluid communication by an opening through the baffle wall. A plurality of extruder tubes extend through the first and second baffle areas and receive the semi-fluid product therethrough. An inlet extends from the first baffle area and permits the introduction of heated fluid, such as water or steam, into the first baffle area. A return outlet is attached from the second baffle area for discharging heated fluid therefrom. The inlet and outlet communicate with the first and second baffle areas, respectively, on opposite sides of the extruder tubes from the opening in the baffle wall through which fluid is communicated from the first baffle area to the second baffle area.

Abstract: A process for the continuous production of a hose formed and vulcanized on a mandrel, comprising continuously forming and advancing a hollow mandrel, continuously forming said hose about said mandrel and continuously vulcanizing said hose while advancing said hose in axial direction with said mandrel, after said mandrel arrives at a predetermined location continuously destroying said mandrel within said hose, and removing the remnants of said mandrel from said hose. The mandrel may be formed of a brittle material such as sintered metal or of a relatively low melting material and its destruction can be effected by longitudinal severance into strips and/or melting by induced current and/or fragmentation by ultrasound. Alternatively the mandrel may be made of soluble material and subsequently dissolved away. Endless reinforcements may also be circulated and the mandrel formed so as to partially embed said reinforcements. Corresponding apparatus is provided.

Abstract: An extrusion die plate and method of making same, the die plate having a die plate body with a die plate face, and a plurality of extrusion passageways in the die plate body terminating generally at the die plate face.

Abstract: An apparatus for melt spinning of polymers into synthetic yarns having greater bundle uniformity has a spinning assembly for extruding molten polymers through orifices in a spinning plate to form filaments and a blow box for directing cooling gas transversely across and through the filaments that extend vertically downwardly from the spinning plates. The spinning plate is provided with at least two groups of orifices and the groups are arranged to provide one or more open lanes or channels that extend across the plate in a direction parallel to the direction of flow of the cooling gas. This lane has a width greater than the distance between adjacent orifices.

Abstract: An assortment of extrusion-puffed dough shapes of varying configurations is produced from a single extruding die assembly by mounting said assembly on a cooker extruder expander adapted to produce a gelatinized cereal dough mass and discharge same as individual moieties sequentially through a plurality of orifices in a backup zone and an extruding zone, the flow rates of said moieties being varied in passage in relationship to the flow characteristics of respective shaping dies by coordinating flow characteristics in respective backup zones so as to cause individual dough masses upon issuance from the face of the assorted extruding die orifices to have extrudates move at comparable linear speed whereby said moieties can be consecutively subdivided by a rotating knife assembly and uniformly puffed, flow coordination being evenly modulated by a substantial buffering zone in a dead space in said cooker.

Abstract: A multiple-cavity extrusion die for coextruding a plurality of indefinite lengths of multiple-layer tubular rubbery material. Core mandrels which extend into openings in the face of the die are adjustable for concentricity with respect to the die by internal or special external adjusting means. Cylindrically shaped core dies have frustro conically shaped forward portions which form extrusion dies with the cores for the core layer of rubbery material and form extrusion dies with a beveled back edge of an adjustable cylindrical cover die. Each of the cover dies is axially adjustable with respect to a respective core die to adjust the speed at which the individual tubes are extruded so that the speed of all tubes can be equalized. Special concentricity plates on the face of the covered dies are adjustably mounted with respect thereto so as to adjust the die openings for concentricity of the cover layer of rubbery material of each tube.

Abstract: The present invention is an improved pellet mill die having tapered grooves along each side of the compression surface of the die. The tapered grooves reduce the stresses at the maximum stress areas and thus control the breakage of metal between the first rows of holes and the inner edges of the grooves.

Abstract: Plug flow of a polymer through a spinneret assembly is approximated by employing an annular inlet means that initially distributes the polymer between the center and the outer wall of a spinneret assembly.

Abstract: A fixed center extruder die assembly is disclosed which serves to apply concentric layers of coating materials on an advancing core wire. The assembly which includes three concentrically arranged and interconnected components comprises an outer die block having a centered first passage with a first axis therethrough; a guiding die with a cylindrical tubing top concentrically disposed with the first passage and second passage therethrough with an axis coincident to the first; and an inner guide having a cylindrical tubing tip and thread passage therethrough which has an axis substantially coincident to the first axis. An improved hand tool is envisioned.

Abstract: A plurality of separate, elongated, metallic members, such as wires, are formed simultaneously, e.g., through the application of hydrostatic extrusion techniques, by passing a single metallic workpiece through a die with a plurality of apertures. The apertures extend longitudinally through the die from an entry wall of the die, and are so arrayed, and the die entry wall includes surfaces which are so configured, as to cooperate to create cross-shear stresses in the material of the workpiece in the vicinity of the apertures. These cross-shear stresses separate, or assist in separating, the workpiece into a plurality of elongated members, so that the forming process may take place at reduced operating pressures.

Abstract: Odor elimination process for plastic film in which at least two extruded plastic films are combined outside of the die. The process utilizes a valve adapting a single extruder to supply two melt streams to a dual melt chamber dual slot die. One melt chamber of the dual slot die is heated to a temperature below the temperature of oxidation of the resin of the thermoplastic material extruded through the die. The other melt chamber is heated above the oxidation temperature of the thermoplastic material extruded through the die, to increase the adhesive qualities of the extruded film to effectively bond with the thermoplastic material heated to a low temperature. The two films are then combined and the high temperature film is sandwiched between the low temperature film and a substrate, trapping the odor of the high temperature film. In a modified form of the invention, the film heated to a high temperature is passed through a tortuous path and heated to its high temperature while passing through this path.

Abstract: An extrusion pack for the production of sheath-core filaments having a high filament density. The pack comprises a stacked assemblage of a stream proportioning means, a stream conjugating means and a spinneret means. The stream conjugating means having upper and lower chambers for forming the sheath-core filaments. The location and spacing of these chambers providing a high filament density.

Abstract: An assortment of extrusion-puffed dough shapes of varying configurations is produced from a single extruding die assembly by mounting said assembly on a cooker extruder expander adapted to produce a gelatinized cereal dough mass and discharge same as individual moieties sequentially through a plurality of orifices in a backup zone and an extruding zone, the flow rates of said moieties being varied in passage in relationship to the flow characteristics of respective shaping dies by coordinating flow characteristics in respective backup zones so as to cause individual dough masses upon issuance from the face of the assorted extruding die orifices to have extrudates move at comparable linear speed whereby said moieties can be consecutively subdivided by a rotating knife assembly and uniformly puffed, flow coordination being evenly modulated by a substantial buffering zone in a dead space in said cooker.

Abstract: An apparatus for melt-spinning a polymer such as a polyamide or polyester has a heating jacket provided with a cavity which accommodates a spinning assembly. Preferably, the spinning assembly is exchangeable in the jacket from above and includes a housing adapted to contain a molten polymer and a spinnerette plate near one end thereof. The opposite end of the housing is closed with a lid which extends partially within the housing and partially outside the housing. That portion of the lid which extends outside the housing has a peripheral surface which slopes radially outwardly from the wall of the housing in the direction moving longitudinally from the housing. In a cylindrical vessel the sloping portion of the lid is frusto-conically shaped. The jacket is provided with a portion of gradually increasing diameter to accommodate the lid.

Abstract: An apparatus for producing composite structure fibers is disclosed which includes an upper distribution plate provided with plural slits for making at least two spinning components into independent thin layer streams, a lower distribution plate provided with plural fine holes for dividing each of said thin layer streams into plural fine capillary streams independent from each other and a spinneret plate provided with a bundling space and extrusion orifices for bundling said previously divided fine capillary streams and extruding them into filaments, said upper distribution plate, lower distribution plate and spinneret plate being piled up in this order.

Abstract: An apparatus for producing a multiple layer conjugate fiber having a housing with a rotary cylinder plug and a stationary spinning plate. The housing is provided with at least two polymer feed inlets and the rotary cylinder plug contains at least two grooves along the outer periphery and passageways in communication with the grooves which open out at the lower surface of the rotary plug. The spinning plate contains a plurality of spinning orifices that are positioned and lined up with the passageways of the rotary cylinder plug. Means are provided for forming a limited space or multiple laminar chamber.

Abstract: A plastic extrusion mechanism having a die head primarily for use in a melt-blown process with the head formed in two mating parts respectively having first and second chambers therein with separate plastic heaters and pressure delivery extruder screws connected thereto and an insulated wall between the chambers with the lower end of the wall having slots leading to passages and alternate passages communicating with the first or second chambers and the passages leading to small extrusion openings for extruding microfibers of plastic and high velocity air directed against the microfibers for attenuation, and a traveling porous surface beneath the die head for receiving the fibers which are formed of plastic from the first chamber having a first physical characteristic and the second chamber having a different physical characteristic.

Abstract: A spinnerette comprising a hollow spinning element having therein a plurality of radially extending spinning apertures positioned in arrays extending around the periphery of the element. A spinning composition forced axially into the spinning element through the ends thereof is extruded by the orifices in radial directions to form filaments.

Abstract: A spinneret assembly for spinning two melts to form three mixed filament yarns per assembly includes a distribution plate which provides a particular metering function to maintain substantially equal deniers for all three yarns and one conveying channel per melt for maintaining substantially equal deniers for all filaments of the same melt within a given yarn.

Abstract: The invention relates to an apparatus and process for producing striated soap bars using a high intensity mixer extruder. A soap mass is levigated and homogenized in a high intensity mixer barrel and forced into a dye injection assembly wherein dye is injected into the soap mass. The soap mass with the injected dye is then forced through conically tapered nozzles to form a striated soap bar.

Abstract: A multiple outlet flat film die apparatus and process which extrude separate streams of material to form any of various composites which may involve joining of similar or dissimilar materials, which includes individual manifold chambers separated from each other by heat insulating means inbetween. The heat insulating means in between such as for example heat insulating material between plates retards heat transfer between the materials. Each manifold is tapered toward its own die mouth; has separate melt inlets adapted for center, top and/or end feed operations; has separate pre-land and final land surfaces leading to individual outlet openings for precise control of melt flow; and has separate heat control means allowing precise temperature control for each melt as it flows toward the die. Temperature differentials may be extensive and may approach the difference between the original temperature of the melt delivered to each manifold. Heat differentials of 0.degree. to 200.degree.F. are an example.

Abstract: A dual outlet extrusion flat film die assembly for various thermo-extrudable materials includes split manifold chambers separated from each other by a rigid centerplate. Each portion of the die in the direction behind the flow materials includes a heat sink slot behind the manifold. Each manifold tapers toward its own die mouth; has separate melt inlets adapted for center, top or end feed operations; has separate pre-land and final land surfaces leading to individual outlet openings for precise control of melt flow; and has separate heat control means allowing precise temperature control for each melt as it flows throughout the die. Temperature differentials ranging from O.degree. to 200.degree.F. are obtainable between the extruded layers. A differential push-pull adjustment system for each movable lip of each outlet opening includes opposed alternatingly staggered thimble bolts to precise control of each individual layer profile.