WO2007124431A2 - Method and apparatus for multi-stream metered extrusion - Google Patents

Method and apparatus for multi-stream metered extrusion Download PDF

Info

Publication number
WO2007124431A2
WO2007124431A2 PCT/US2007/067106 US2007067106W WO2007124431A2 WO 2007124431 A2 WO2007124431 A2 WO 2007124431A2 US 2007067106 W US2007067106 W US 2007067106W WO 2007124431 A2 WO2007124431 A2 WO 2007124431A2
Authority
WO
WIPO (PCT)
Prior art keywords
flow
coating
extrusion
planetary gear
gear pump
Prior art date
Application number
PCT/US2007/067106
Other languages
French (fr)
Other versions
WO2007124431A3 (en
Inventor
Stephen Spruell
Original Assignee
Southwire Company
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Southwire Company filed Critical Southwire Company
Priority to MX2008013490A priority Critical patent/MX2008013490A/en
Priority to EP07761030.1A priority patent/EP2012911A4/en
Priority to CA002649308A priority patent/CA2649308A1/en
Publication of WO2007124431A2 publication Critical patent/WO2007124431A2/en
Publication of WO2007124431A3 publication Critical patent/WO2007124431A3/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/465Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using rollers
    • B29C48/467Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using rollers using single rollers, e.g. provided with protrusions, closely surrounded by a housing with movement of the material in the axial direction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/15Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor incorporating preformed parts or layers, e.g. extrusion moulding around inserts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/16Articles comprising two or more components, e.g. co-extruded layers
    • B29C48/18Articles comprising two or more components, e.g. co-extruded layers the components being layers
    • B29C48/19Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their edges
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/365Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pumps, e.g. piston pumps
    • B29C48/37Gear pumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/387Plasticisers, homogenisers or feeders comprising two or more stages using a screw extruder and a gear pump
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/9258Velocity
    • B29C2948/926Flow or feed rate
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92609Dimensions
    • B29C2948/92647Thickness
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/05Filamentary, e.g. strands
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/06Rod-shaped
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/15Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor incorporating preformed parts or layers, e.g. extrusion moulding around inserts
    • B29C48/154Coating solid articles, i.e. non-hollow articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/16Articles comprising two or more components, e.g. co-extruded layers
    • B29C48/17Articles comprising two or more components, e.g. co-extruded layers the components having different colours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/16Articles comprising two or more components, e.g. co-extruded layers
    • B29C48/18Articles comprising two or more components, e.g. co-extruded layers the components being layers
    • B29C48/21Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/32Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
    • B29C48/34Cross-head annular extrusion nozzles, i.e. for simultaneously receiving moulding material and the preform to be coated
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/49Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using two or more extruders to feed one die or nozzle
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/695Flow dividers, e.g. breaker plates
    • B29C48/70Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows
    • B29C48/705Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows in the die zone, e.g. to create flow homogeneity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C2/00Rotary-piston machines or pumps
    • F04C2/08Rotary-piston machines or pumps of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C2220/00Application
    • F04C2220/24Application for metering throughflow

Definitions

  • the invention relates to extrusion of various materials in the manufacture of extruded products and in the application of a coating layer or layers to a substrate.
  • metal wire such as conductors in electrical cables
  • metal wire are typically extruded in moving production lines with one or more polymer layers as insulators, sealants and the like. It is advantageous in the coating of wire or other substrates to apply a uniform thickness of coating material around a substrate's surface. Beyond undesired aesthetics and potential adverse effect on the use of the end-product, non-uniform application of coating materials results in wasted coating material and undesired costs.
  • the invention provides an extrusion method of providing a plurality of metered individual streams of extrusion material to an extrusion head, joining the individual streams from expansion regions of a flow joiner into a flow with uniform thickness at a tapered surface of the extrusion head and extruding the flow as an extruded end-product or as a coating on to a substrate.
  • the flow is annular.
  • the metered individual streams are provided from one or more planetary and/or non-planetary gear pumps, including spur and helical gear pumps.
  • a planetary gear pump includes two or more stream outlets to provide metered extrusion material.
  • multiple single-stream non-planetary gear pumps may also be used to provide multiple metered streams that combine into a uniform annular flow. It will be appreciated that planetary gear pumps permit precise metering of dependent outlet streams with a common central gear in embodiments of the invention, but multiple single-stream non- planetary gear pumps with independent streams also provide beneficial metering in other embodiments of the invention. In some embodiments, both planetary and non- planetary gear pumps may be used together.
  • one or more individual streams include a color different from one or more other individual streams. Such coloring may be used as striping, including in cable products and the like.
  • different streams may comprise different materials to provide desired properties in different areas of the end product or on a substrate.
  • multiple flows may be used by joining a second coating flow of uniform thickness on a second tapered surface of the extrusion head and extruding the second coating flow on to an underlying coating flow and extruding multiple layers of coating on to a substrate.
  • the invention provides a method for extrusion that includes providing a plurality of metered individual streams of extrusion material from one or more planetary gear pumps to an extrusion head, joining the individual streams into an annular flow with uniform thickness at a tapered surface of the extrusion head and extruding the flow.
  • the flow may be extruded as end product, such as tubing, piping, hoses, and the like, or for coating a substrate, such as in cables, wire, cables, pipe, foodstuffs, poles, rods, tubing, fibers, fiber optics, chains, shafts and the like.
  • the invention provides an extrusion apparatus comprising a flow joiner including a plurality of extrusion material inlets communicating with a plurality of expansion regions that expand to a tapered annular surface.
  • a plurality of planetary gear pump outlets are coupled to the plurality of extrusion material inlets of the flow joiner, such as with hoses or via channels in a manifold.
  • the planetary gear pump may be included with a through-bore allowing passage of a substrate, or the gear pump may be out-of-line with the extrusion head and without a through-bore.
  • FIG. 1 is a basic schematic diagram depicting a planetary gear pump coupled to an extrusion head with connection hoses in an embodiment of the invention.
  • FIG. 2A is a basic schematic diagram depicting a planetary gear pump coupled to an extrusion flange and an extrusion head with a manifold in an embodiment of the invention.
  • FIG. 2B is a basic schematic diagram depicting a planetary gear pump coupled to an extrusion head with a manifold in an embodiment of the invention.
  • FIG. 3 is a front perspective view from above of a manifold in an embodiment of the invention.
  • FIG. 4 is a front transparent perspective view of a manifold in an embodiment of the invention.
  • FIG. 5 is a front perspective cross-sectional view from above of a manifold in an embodiment of the invention.
  • FIG. 6 is a perspective side view from the rear of a manifold in an embodiment of the invention.
  • FIG. 7 is a basic schematic cross-sectional diagram depicting an extrusion head in an embodiment of the invention.
  • FIG. 8 is a front perspective view depicting a flow joiner in an embodiment of the invention.
  • FIG. 9 is side view of a flow joiner in an embodiment of the invention.
  • FIG. 10 is a front perspective view depicting an extrusion die in an embodiment of the invention.
  • FIG. 11 is a front perspective view depicting an extrusion tip in an embodiment of the invention.
  • FIG. 12 is a front perspective view of an extrusion head, through-bore planetary gear pump and through-bore gear box illustrating a tip and die end in an embodiment of the invention.
  • FIG. 13 is a rear perspective view of an extrusion head, through-bore planetary gear pump and through-bore gear box illustrating a through-bore gear box end in an embodiment of the invention.
  • FIG. 14 is a basic schematic diagram of a planetary gear pump with a central gear and six planet gears in an embodiment of the invention.
  • FIG. 15 is a basic schematic diagram of a through-bore planetary gear pump with a central gear and six planet gears in an embodiment of the invention.
  • FIG. 16 is a basic schematic diagram depicting a single-stream gear pump coupled between an extruder and a planetary gear pump that is coupled to an extrusion head with a manifold in an embodiment of the invention.
  • an apparatus and method for coating substrates including moving substrates in a production line, such as, but not limited to, wire, cables, pipe, foodstuffs, poles, rods, tubing, fibers, fiber optics, chains, shafts, and other items of manufacture, is provided. While the invention is described in one embodiment with respect to coating bare metal wire conductors or cable assemblies with plastic insulating materials, it will be appreciated that the invention is not intended to be limited thereto, and may be employed for coating a wide variety of substrates of different materials, with a wide variety of coatings of materials. Numerous applications ranging widely from coating metal wire with plastic insulating material to coating pretzels sticks with chocolate may be encompassed by the invention without limitation.
  • coating materials may include rubber, polyethylene, polyvinyl chloride, chlorosulfonated polyethylene, polypropylene, nylon, fiberglass, chloropolyethylene, polychlorprene, neoprene, vinyl and silane-crosslinked polyethylene. Combinations of these and other materials, including plastics (including thermoset and thermoplastic), polymers (including cross-linkable and non-cross-linkable), synthetic and natural materials may also be used in other embodiments of the invention.
  • annular extrusion head for coating cylindrical substrates of different sizes
  • the invention might be similarly applied with other substrate shapes and extrusion head shapes, including, but not limited to polygons of many different shapes (and number of sides) and sizes.
  • a planetary gear pump 10 is coupled to an extrusion head 70.
  • a planetary gear pump 10 in one embodiment provides six streams with six inlets 13 and six outlets 14, with one pair of inlet 13 and outlet 14 associated with each planetary gear 11. In other embodiments, other numbers of planetary gears 11 and inlet/outlet streams may be used.
  • FIG. 15 depicts a planetary gear pump 10 with a pump through-bore 15 for passage of a substrate through the gear pump 10.
  • An input shaft 20 drives central gear 17.
  • Extrusion material enters the gear pump 10 into pump material inlet 30 via a connector 40 to an extrusion material supply and the extrusion material exits outlets 14 as it is precisely metered through the gear pump 10 by the central gear 17 rotating the planetary gears 11.
  • a connection tube or hose 60 directs the precisely metered separate individual streams from outlets 50 in the gear pump 10 to stream inlets 75 of the extrusion head 70.
  • FIGS. 2A and 2B Another alternate arrangement is shown in FIGS. 2A and 2B, utilizing a manifold 140 instead of tubes or hoses (FIG. 1 ).
  • the planetary gear pump 10 is driven by the input shaft 20.
  • An exemplary planetary gear pump includes a six-stream HSG- style planetary polymer melt gear pump with 60cc/Rev/stream from Zenith Pumps (Sanford, N. C), a division of Colfax Corporation.
  • a motor- driven single-stream gear pump 11 may be coupled between an extruder 65 and planetary gear pump 10.
  • the planetary gear pump 10 is coupled to manifold 140 and extrusion head 70.
  • Extrusion flange 45 is coupled to an outlet of the single-stream gear pump 18 to receive a metered flow of material that is delivered via the manifold 140 to planetary gear pump 10 for producing multiple streams to the extrusion head 70.
  • Centering line 72 depicts the line of a travel of a substrate (or direction of extrusion of an end product) with respect to extrusion head 70.
  • the metered flow from single stream gear pump 11 drives planetary gear pump 10 without requiring a drive shaft 20 (FIGS. 2A and 2B). In other embodiments both a single stream pump 11 and planetary gear pump 10 may be driven to maintain metered flow.
  • extrusion material enters a heated manifold 140 from the extruder flange connection 45 coupled to manifold inlet 43.
  • machined channels 80 in the face of the manifold 140 couple to extrusion head 70.
  • extrusion head stream inlets 75 receive separate individual streams of metered extrusion material from channels 80 in embodiments where the manifold 140 is coupled to the extrusion head 70 instead of hoses.
  • a manifold through-bore 150 in the manifold 140 provides for passage of the substrate through the manifold 140 and into a coupled extrusion head 70.
  • 83 connects manifold inlet 43 to deliver extrusion material into the planetary gear pump 10 coupling pump material inlet 30 (FIG. 1 ) to manifold pump opening 44.
  • the manifold 140 bolts at connection points 57 to the planetary gear pump 10 as shown in FIGS. 2A and 2B.
  • Metered material exits the planetary gear pump 10 from outlets 14 and to outlets 50 (FIG. 1 ) that are coupled to gear pump outlet openings 46 in the manifold 140.
  • Machined ports 82 deliver the metered material from the planetary gear pump 10 through the manifold 140 to the machine channels 80 that couple to extrusion head 70.
  • Adjustment points 58 provide for adjustment of tip location.
  • a thermocouple port 59 allows for monitoring temperature. It will be appreciated that in some embodiments of the invention wrap-around cylindrical heater bands known in the art can be used to maintain the desired temperature levels of equipment.
  • FIG. 7 A cross-section of an extrusion head 70 is shown in FIG. 7.
  • a flow joiner 70 A flow joiner
  • FIGS. 8 and 9 takes the six precisely metered streams of extrusion material from extrusion head inlets 75 (FIG. 1 ) and gradually combines them into a precise annular ring with uniform thickness around the entire cylindrical extruded volume.
  • a die holder 120 holds the extrusion die 130, shown in FIG. 10, which sizes the extruded coating over the cable.
  • a die retainer 170 maintains the die in the correct position.
  • An extrusion tip 110 shown in FIG. 11 , guides the substrate to be coated, as the coating material is uniformly deposited on the substrate passed through.
  • metered extrusion compound enters into regions 101 of flow joiner 100 and is then gradually squeezed in expansion regions 102 and then joins at annular space 103 and travels down adjacent tapered region 104.
  • the extrusion compound e.g. coating material
  • flow joiner 100 includes milled regions 101 with approximately 5/32" radius with a 1/32 x 45° chamfered edge 107.
  • Tapered region 104 slopes at an angle of approximately 30°, and the opening 108 has a diameter of approximately 5.335".
  • Region 103 is approximately .487" long
  • tapered region 104 is approximately 1.1013" long
  • the expansion region 102 (from outlet of region 101 to region 103) is approximately 1 3/4" long.
  • the overall length of the flow joiner 100 in one embodiment is 7.025" long. It will be appreciated that in other embodiments different dimensions and sized components can be used to accommodate various substrates and extruded products without departing from the invention.
  • a planetary gear pump is provided with a pump through-bore 15 and coupled in-line to the extrusion head 70.
  • Drive shaft 20 drives gear box 12 coupled to planetary gear pump 10.
  • the substrate passes through the pump through-bore 15 of the planetary gear pump 10 and through the tip 110 and die 130 of the extrusion head 70 for coating.
  • a planetary gear pump 10 provides multiple streams of flowing coating material to an extrusion head 70 for precise deposition of the coating material onto a desired substrate.
  • the coating apparatus and method of the invention may be utilized in a wide-ranging variety of applications, and the rates of coating flow, substrate delivery speed rate, types of coatings and substrate materials, coating material temperatures and sizes and shapes of substrates may vary based on the desired coated end products.
  • the multiple metered streams from the planetary gear pump are joined, such as with an annular flow joiner 100 in a described embodiment, with continued flow of the coating material over an extrusion tip 110 and on to the substrate that passes through a die 130.
  • the use of a planetary gear pump 10 and multiple, metered streams provides a coating process for uniform thickness with less material coating waste (such as build up in areas of the coating layer that may occur in prior art methods), more uniform coated end product, less machinery and other advantages.
  • the use of multiple streams permits streams of different materials and/or colorings to be applied to the substrate.
  • one or more streams provided from the planetary gear pump to the extrusion head and deposited for coating on the substrate might be colored striping such as on an insulated wire cable.
  • striping or other desired regions of the coated substrate might be formed with different materials in different individual streams provided from the planetary gear pump.
  • a plurality of planetary or non-planetary gear pumps, including single stream pumps, may be utilized to provide multiple streams to an extrusion head.
  • multiple planetary gear pumps and multiple extrusion heads may be used to provide multiple layers of coatings.
  • subsequent coating processes may be implemented, where a first coating is applied to a substrate and "down the line" a second coating (such as further reinforcement or of other material) is subsequently applied to the substrate.
  • extrusion heads or internal channels therein may be "nested” so that a plurality of layers of coatings (such as of different materials) are simultaneously applied at the extrusion tip.
  • a first coating flow layer underlies a second flowing layer for deposition of multiple layers on the substrate.
  • sealant, reinforcing and other intermediate layers may be deposited as underlying coating layers.
  • multiple single-stream non-planetary gear pumps may be connected via hoses or manifold to provide multiple metered streams to an extrusion head.
  • combinations of single-stream gear pumps and multi-stream planetary gear pumps may be utilized to provide multiple streams to an extrusion head, including, but not limited to, providing a variety of materials, colorings or multi-layer nesting extrusion embodiments.
  • the invention may be used to produce extruded product without coating a substrate, such as hoses, tubing, piping, conduit, foodstuffs and other annular-shaped products. It will be appreciated that in these embodiments, the product material itself is extruded from the tip and die similar to the extrusion of coating in coating embodiments. The extruded material is permitted to harden and/or cure into the desired end product.
  • a substrate such as hoses, tubing, piping, conduit, foodstuffs and other annular-shaped products.

Abstract

An extrusion apparatus for extruding multiple streams of extrusion material as extruded end-products and in the coating of substrates. A flow joiner in an extrusion head combines multiple metered streams, such as from a gear pump, into a uniform extrusion flow.

Description

Method and Apparatus for Multi-Stream Metered Extrusion
Technical Field
[0001] The invention relates to extrusion of various materials in the manufacture of extruded products and in the application of a coating layer or layers to a substrate.
[0002] In one example of an extrusion application, metal wire, such as conductors in electrical cables, are typically extruded in moving production lines with one or more polymer layers as insulators, sealants and the like. It is advantageous in the coating of wire or other substrates to apply a uniform thickness of coating material around a substrate's surface. Beyond undesired aesthetics and potential adverse effect on the use of the end-product, non-uniform application of coating materials results in wasted coating material and undesired costs.
Disclosure of the Invention
[0003] In one embodiment, the invention provides an extrusion method of providing a plurality of metered individual streams of extrusion material to an extrusion head, joining the individual streams from expansion regions of a flow joiner into a flow with uniform thickness at a tapered surface of the extrusion head and extruding the flow as an extruded end-product or as a coating on to a substrate. In various embodiments, the flow is annular. In various embodiments, the metered individual streams are provided from one or more planetary and/or non-planetary gear pumps, including spur and helical gear pumps.
[0004] In embodiments of the invention, a planetary gear pump includes two or more stream outlets to provide metered extrusion material. In other embodiments, multiple single-stream non-planetary gear pumps may also be used to provide multiple metered streams that combine into a uniform annular flow. It will be appreciated that planetary gear pumps permit precise metering of dependent outlet streams with a common central gear in embodiments of the invention, but multiple single-stream non- planetary gear pumps with independent streams also provide beneficial metering in other embodiments of the invention. In some embodiments, both planetary and non- planetary gear pumps may be used together.
[0005] In some embodiments of the invention, one or more individual streams include a color different from one or more other individual streams. Such coloring may be used as striping, including in cable products and the like. In other embodiments, different streams may comprise different materials to provide desired properties in different areas of the end product or on a substrate.
[0006] In some embodiments multiple flows may be used by joining a second coating flow of uniform thickness on a second tapered surface of the extrusion head and extruding the second coating flow on to an underlying coating flow and extruding multiple layers of coating on to a substrate.
[0007] In another embodiment, the invention provides a method for extrusion that includes providing a plurality of metered individual streams of extrusion material from one or more planetary gear pumps to an extrusion head, joining the individual streams into an annular flow with uniform thickness at a tapered surface of the extrusion head and extruding the flow. The flow may be extruded as end product, such as tubing, piping, hoses, and the like, or for coating a substrate, such as in cables, wire, cables, pipe, foodstuffs, poles, rods, tubing, fibers, fiber optics, chains, shafts and the like.
[0008] In further embodiments, the invention provides an extrusion apparatus comprising a flow joiner including a plurality of extrusion material inlets communicating with a plurality of expansion regions that expand to a tapered annular surface. In some embodiments a plurality of planetary gear pump outlets are coupled to the plurality of extrusion material inlets of the flow joiner, such as with hoses or via channels in a manifold.
[0009] In embodiments of the invention using a planetary gear pump, the planetary gear pump may be included with a through-bore allowing passage of a substrate, or the gear pump may be out-of-line with the extrusion head and without a through-bore. Brief Description of the Drawings
[0010] FIG. 1 is a basic schematic diagram depicting a planetary gear pump coupled to an extrusion head with connection hoses in an embodiment of the invention.
[0011] FIG. 2A is a basic schematic diagram depicting a planetary gear pump coupled to an extrusion flange and an extrusion head with a manifold in an embodiment of the invention.
[0012] FIG. 2B is a basic schematic diagram depicting a planetary gear pump coupled to an extrusion head with a manifold in an embodiment of the invention.
[0013] FIG. 3 is a front perspective view from above of a manifold in an embodiment of the invention.
[0014] FIG. 4 is a front transparent perspective view of a manifold in an embodiment of the invention.
[0015] FIG. 5 is a front perspective cross-sectional view from above of a manifold in an embodiment of the invention.
[0016] FIG. 6 is a perspective side view from the rear of a manifold in an embodiment of the invention.
[0017] FIG. 7 is a basic schematic cross-sectional diagram depicting an extrusion head in an embodiment of the invention.
[0018] FIG. 8 is a front perspective view depicting a flow joiner in an embodiment of the invention.
[0019] FIG. 9 is side view of a flow joiner in an embodiment of the invention.
[0020] FIG. 10 is a front perspective view depicting an extrusion die in an embodiment of the invention.
[0021] FIG. 11 is a front perspective view depicting an extrusion tip in an embodiment of the invention. [0022] FIG. 12 is a front perspective view of an extrusion head, through-bore planetary gear pump and through-bore gear box illustrating a tip and die end in an embodiment of the invention.
[0023] FIG. 13 is a rear perspective view of an extrusion head, through-bore planetary gear pump and through-bore gear box illustrating a through-bore gear box end in an embodiment of the invention.
[0024] FIG. 14 is a basic schematic diagram of a planetary gear pump with a central gear and six planet gears in an embodiment of the invention.
[0025] FIG. 15 is a basic schematic diagram of a through-bore planetary gear pump with a central gear and six planet gears in an embodiment of the invention.
[0026] FIG. 16 is a basic schematic diagram depicting a single-stream gear pump coupled between an extruder and a planetary gear pump that is coupled to an extrusion head with a manifold in an embodiment of the invention.
Best Mode for Carrying Out the Invention
[0027] Embodiments of the invention will be described with reference to the accompanying drawings and figures wherein like numbers represent like elements throughout. Further, it is to be understood that the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting. The use of "including", "comprising", or "having" and variations thereof herein is meant to encompass the items listed thereafter and equivalents thereof as well as additional items. The terms "mounted", "connected", and "coupled" are used broadly and encompass both direct and indirect mounting, connecting, binding and coupling. Further, "connected" and "coupled" are not restricted to physical or mechanical connections, bindings or couplings.
[0028] As more fully described subsequently with reference to the drawings, in one embodiment an apparatus and method for coating substrates, including moving substrates in a production line, such as, but not limited to, wire, cables, pipe, foodstuffs, poles, rods, tubing, fibers, fiber optics, chains, shafts, and other items of manufacture, is provided. While the invention is described in one embodiment with respect to coating bare metal wire conductors or cable assemblies with plastic insulating materials, it will be appreciated that the invention is not intended to be limited thereto, and may be employed for coating a wide variety of substrates of different materials, with a wide variety of coatings of materials. Numerous applications ranging widely from coating metal wire with plastic insulating material to coating pretzels sticks with chocolate may be encompassed by the invention without limitation.
[0029] In embodiments where wire conductors are provided as a substrate, such as in the production of insulated electrical cables, including low, medium and high voltage cables, coating materials may include rubber, polyethylene, polyvinyl chloride, chlorosulfonated polyethylene, polypropylene, nylon, fiberglass, chloropolyethylene, polychlorprene, neoprene, vinyl and silane-crosslinked polyethylene. Combinations of these and other materials, including plastics (including thermoset and thermoplastic), polymers (including cross-linkable and non-cross-linkable), synthetic and natural materials may also be used in other embodiments of the invention.
[0030] Further, it will be appreciated, that while one described embodiment includes an annular extrusion head for coating cylindrical substrates of different sizes, the invention might be similarly applied with other substrate shapes and extrusion head shapes, including, but not limited to polygons of many different shapes (and number of sides) and sizes.
[0031] Referring to FIGS. 1 , 14 and 15, in one embodiment of the invention, a planetary gear pump 10, is coupled to an extrusion head 70. A planetary gear pump 10 in one embodiment provides six streams with six inlets 13 and six outlets 14, with one pair of inlet 13 and outlet 14 associated with each planetary gear 11. In other embodiments, other numbers of planetary gears 11 and inlet/outlet streams may be used. FIG. 15 depicts a planetary gear pump 10 with a pump through-bore 15 for passage of a substrate through the gear pump 10.
[0032] An input shaft 20 drives central gear 17. Extrusion material enters the gear pump 10 into pump material inlet 30 via a connector 40 to an extrusion material supply and the extrusion material exits outlets 14 as it is precisely metered through the gear pump 10 by the central gear 17 rotating the planetary gears 11. A connection tube or hose 60 directs the precisely metered separate individual streams from outlets 50 in the gear pump 10 to stream inlets 75 of the extrusion head 70.
[0033] Another alternate arrangement is shown in FIGS. 2A and 2B, utilizing a manifold 140 instead of tubes or hoses (FIG. 1 ). The planetary gear pump 10 is driven by the input shaft 20. An exemplary planetary gear pump includes a six-stream HSG- style planetary polymer melt gear pump with 60cc/Rev/stream from Zenith Pumps (Sanford, N. C), a division of Colfax Corporation.
[0034] Referring to FIG. 16, in another embodiment of the invention, a motor- driven single-stream gear pump 11 may be coupled between an extruder 65 and planetary gear pump 10. As shown in FIG. 16, the planetary gear pump 10 is coupled to manifold 140 and extrusion head 70. Extrusion flange 45 is coupled to an outlet of the single-stream gear pump 18 to receive a metered flow of material that is delivered via the manifold 140 to planetary gear pump 10 for producing multiple streams to the extrusion head 70. Centering line 72 depicts the line of a travel of a substrate (or direction of extrusion of an end product) with respect to extrusion head 70. In embodiments, the metered flow from single stream gear pump 11 drives planetary gear pump 10 without requiring a drive shaft 20 (FIGS. 2A and 2B). In other embodiments both a single stream pump 11 and planetary gear pump 10 may be driven to maintain metered flow.
[0035] With further reference to FIGS. 3-6, extrusion material enters a heated manifold 140 from the extruder flange connection 45 coupled to manifold inlet 43. As shown in FIGS. 3 and 4, machined channels 80 in the face of the manifold 140 couple to extrusion head 70. With further reference to FIG. 1 , extrusion head stream inlets 75 receive separate individual streams of metered extrusion material from channels 80 in embodiments where the manifold 140 is coupled to the extrusion head 70 instead of hoses.
[0036] With continuing reference to FIG. 4, and further reference to FIG. 5, ports
82 in the manifold 140 deliver material to the planetary gear pump 10 and also deliver the metered output streams from outlets 14 of the planetary gear pump 10 to the extrusion head 70 at channels 80 in preparation for producing a precise dimensional annular ring of uniform thickness. A manifold through-bore 150 in the manifold 140 provides for passage of the substrate through the manifold 140 and into a coupled extrusion head 70.
[0037] With specific reference to FIGS. 2A and 2B, 3-6 and 14, a machined port
83 connects manifold inlet 43 to deliver extrusion material into the planetary gear pump 10 coupling pump material inlet 30 (FIG. 1 ) to manifold pump opening 44. The manifold 140 bolts at connection points 57 to the planetary gear pump 10 as shown in FIGS. 2A and 2B. Metered material exits the planetary gear pump 10 from outlets 14 and to outlets 50 (FIG. 1 ) that are coupled to gear pump outlet openings 46 in the manifold 140. Machined ports 82 deliver the metered material from the planetary gear pump 10 through the manifold 140 to the machine channels 80 that couple to extrusion head 70. Adjustment points 58 provide for adjustment of tip location. A thermocouple port 59 allows for monitoring temperature. It will be appreciated that in some embodiments of the invention wrap-around cylindrical heater bands known in the art can be used to maintain the desired temperature levels of equipment.
[0038] A cross-section of an extrusion head 70 is shown in FIG. 7. A flow joiner
100, shown in FIGS. 8 and 9, takes the six precisely metered streams of extrusion material from extrusion head inlets 75 (FIG. 1 ) and gradually combines them into a precise annular ring with uniform thickness around the entire cylindrical extruded volume. A die holder 120 holds the extrusion die 130, shown in FIG. 10, which sizes the extruded coating over the cable. A die retainer 170 maintains the die in the correct position. An extrusion tip 110, shown in FIG. 11 , guides the substrate to be coated, as the coating material is uniformly deposited on the substrate passed through.
[0039] With continuing reference to FIGS. 8 and 9, metered extrusion compound enters into regions 101 of flow joiner 100 and is then gradually squeezed in expansion regions 102 and then joins at annular space 103 and travels down adjacent tapered region 104. Metered from the planetary gear pump 10, the extrusion compound, e.g. coating material, is deposited on to the substrate passing through the tip (FIG. 11 ) and die (FIG. 10) in a uniform, annular application. [0040] In one embodiment for extruding a substrate of 3/4" to about 2" in diameter, flow joiner 100 includes milled regions 101 with approximately 5/32" radius with a 1/32 x 45° chamfered edge 107. Tapered region 104 slopes at an angle of approximately 30°, and the opening 108 has a diameter of approximately 5.335". Region 103 is approximately .487" long, tapered region 104 is approximately 1.1013" long and the expansion region 102 (from outlet of region 101 to region 103) is approximately 1 3/4" long. The overall length of the flow joiner 100 in one embodiment is 7.025" long. It will be appreciated that in other embodiments different dimensions and sized components can be used to accommodate various substrates and extruded products without departing from the invention.
[0041] Referring to FIGS. 12, 13 and 15, in another embodiment of the invention, a planetary gear pump is provided with a pump through-bore 15 and coupled in-line to the extrusion head 70. Drive shaft 20 drives gear box 12 coupled to planetary gear pump 10. The substrate passes through the pump through-bore 15 of the planetary gear pump 10 and through the tip 110 and die 130 of the extrusion head 70 for coating.
[0042] In embodiments of the invention, a planetary gear pump 10 provides multiple streams of flowing coating material to an extrusion head 70 for precise deposition of the coating material onto a desired substrate. As described, the coating apparatus and method of the invention may be utilized in a wide-ranging variety of applications, and the rates of coating flow, substrate delivery speed rate, types of coatings and substrate materials, coating material temperatures and sizes and shapes of substrates may vary based on the desired coated end products.
[0043] At the extrusion head 70, the multiple metered streams from the planetary gear pump are joined, such as with an annular flow joiner 100 in a described embodiment, with continued flow of the coating material over an extrusion tip 110 and on to the substrate that passes through a die 130. The use of a planetary gear pump 10 and multiple, metered streams, provides a coating process for uniform thickness with less material coating waste (such as build up in areas of the coating layer that may occur in prior art methods), more uniform coated end product, less machinery and other advantages. [0044] Further, the use of multiple streams permits streams of different materials and/or colorings to be applied to the substrate. In one example, one or more streams provided from the planetary gear pump to the extrusion head and deposited for coating on the substrate, might be colored striping such as on an insulated wire cable. In other embodiments, such striping or other desired regions of the coated substrate might be formed with different materials in different individual streams provided from the planetary gear pump. In other embodiments, a plurality of planetary or non-planetary gear pumps, including single stream pumps, may be utilized to provide multiple streams to an extrusion head.
[0045] In still other embodiments of the invention, multiple planetary gear pumps and multiple extrusion heads may be used to provide multiple layers of coatings. For example, subsequent coating processes may be implemented, where a first coating is applied to a substrate and "down the line" a second coating (such as further reinforcement or of other material) is subsequently applied to the substrate. In alternative embodiments, extrusion heads (or internal channels therein) may be "nested" so that a plurality of layers of coatings (such as of different materials) are simultaneously applied at the extrusion tip. In such embodiments, a first coating flow layer underlies a second flowing layer for deposition of multiple layers on the substrate. In these and other embodiments, sealant, reinforcing and other intermediate layers may be deposited as underlying coating layers.
[0046] In other embodiments, multiple single-stream non-planetary gear pumps may be connected via hoses or manifold to provide multiple metered streams to an extrusion head. In other embodiments, combinations of single-stream gear pumps and multi-stream planetary gear pumps may be utilized to provide multiple streams to an extrusion head, including, but not limited to, providing a variety of materials, colorings or multi-layer nesting extrusion embodiments.
[0047] In other embodiments, the invention may be used to produce extruded product without coating a substrate, such as hoses, tubing, piping, conduit, foodstuffs and other annular-shaped products. It will be appreciated that in these embodiments, the product material itself is extruded from the tip and die similar to the extrusion of coating in coating embodiments. The extruded material is permitted to harden and/or cure into the desired end product.
[0048] It will also be appreciated that other shapes, including polygons of many different shapes (and number of sides) and sizes could be extruded with the desired shape of flow joiner and tip and die configuration.
[0049] Although the invention herein has been described with reference to particular embodiments, it is to be understood that these embodiments are merely illustrative of the principals and applications of the invention. Accordingly, while the invention has been described with reference to the structures and processes disclosed, it is not confined to the details set forth, but is intended to cover such modifications or changes as may fall within the scope of the following claims.

Claims

CLAIMSWhat is claimed is:
1. A method for coating a substrate comprising: providing a plurality of metered, separate individual streams of coating material to an extrusion head; joining the individual streams from expansion regions of a flow joiner into a coating flow with uniform thickness at an annular surface region of the flow joiner; and extruding the coating flow on to a substrate.
2. The method of claim 1 , wherein the coating flow is an annular flow.
3. The method of claim 2, wherein the substrate is cylindrical.
4. The method of claim 1 , wherein one or more individual streams include a color different from one or more other individual streams.
5. The method of claim 1 , wherein at least two individual streams each include a different coating material.
6. The method of claim 1 further comprising joining a second coating flow of uniform thickness on a second tapered surface of the extrusion head, extruding the second coating flow on to an underlying coating flow and extruding multiple layers of coating on to the substrate.
7. The method of claim 1 , wherein the substrate is metal conductor core and the coating material is an insulation layer.
8. The method of claim 1 , further comprising pumping the individual streams of coating material from one or more gear pumps to the extrusion head.
9. The method of claim 8, wherein the one or more gear pumps includes a planetary gear pump.
10. The method of claim 8, wherein the one or more gear pumps include a plurality of non-planetary gear pumps.
11. The method of claim 8, wherein the one or more gear pumps include at least one planetary gear pump and at least one non-planetary gear pump.
12. A method for extrusion comprising: providing a plurality of metered, separate individual streams of extrusion material from one or more gear pumps to an extrusion head; joining the individual streams into an annular flow with uniform thickness; tapering the annular flow to a tip and die; and extruding the annular flow.
13. The method of claim 12 further comprising extruding the flow as a coating material on a substrate.
14. The method of claim 13, wherein the substrate is metal conductor core and the coating material is an insulation layer.
15. The method of claim 12, wherein one or more individual streams include a color different from one or more other individual streams.
16. The method of claim 12, wherein at least two individual streams each include a different extrusion material.
17. The method of claim 12, further comprising joining a second annular flow of uniform thickness on a second tapered surface of the extrusion head, extruding the second annular flow on to an underlying annular flow and extruding multiple layers of extrusion material.
18. The method of claim 12, further comprising extruding the flow as an annular end- product selected from the group consisting of a hose, tube, conduit, pole and pipe.
19. The method of claim 12, further comprising metering the flow of individual streams with one or more gear pumps selected from the group consisting of a non-planetary and planetary gear pump.
20. An extrusion apparatus comprising a plurality of individual stream inlets coupled to a flow joiner, wherein the flow joiner includes a plurality of extrusion material inlets communicating with a plurality of expansion regions that expand to an annular surface region communicating with a downstream tapered region..
21. The apparatus of claim 20 further comprising one or more gear pumps coupled to the individual stream inlets, wherein the one or more gear pumps include a gear pump selected from the group consisting of a planetary gear pump and non- planetary gear pump.
22. The apparatus of claim 21 further comprising a plurality of hoses connecting the one or more gear pumps to the plurality of individual stream inlets.
23. The apparatus of claim 21 further comprising a manifold including ports connecting the one or more gear pumps to the individual stream inlets.
24. The apparatus of claim 21 further comprising a planetary gear pump with a through-bore.
PCT/US2007/067106 2006-04-21 2007-04-20 Method and apparatus for multi-stream metered extrusion WO2007124431A2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
MX2008013490A MX2008013490A (en) 2006-04-21 2007-04-20 Method and apparatus for multi-stream metered extrusion.
EP07761030.1A EP2012911A4 (en) 2006-04-21 2007-04-20 Method and apparatus for multi-stream metered extrusion
CA002649308A CA2649308A1 (en) 2006-04-21 2007-04-20 Method and apparatus for multi-stream metered extrusion

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US79425706P 2006-04-21 2006-04-21
US60/794,257 2006-04-21
US82780106P 2006-10-02 2006-10-02
US60/827,801 2006-10-02

Publications (2)

Publication Number Publication Date
WO2007124431A2 true WO2007124431A2 (en) 2007-11-01
WO2007124431A3 WO2007124431A3 (en) 2008-03-27

Family

ID=38625771

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2007/067106 WO2007124431A2 (en) 2006-04-21 2007-04-20 Method and apparatus for multi-stream metered extrusion

Country Status (5)

Country Link
US (2) US7754124B2 (en)
EP (1) EP2012911A4 (en)
CA (1) CA2649308A1 (en)
MX (1) MX2008013490A (en)
WO (1) WO2007124431A2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2649308A1 (en) * 2006-04-21 2007-11-01 Southwire Company Method and apparatus for multi-stream metered extrusion
US8827676B1 (en) 2012-03-02 2014-09-09 Encore Wire Corporation Apparatus and method for extruding stripes onto an extruded product
CA2903820C (en) 2013-03-15 2021-04-20 Mars, Incorporated Extruder system and method

Family Cites Families (69)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1785386A (en) 1927-09-08 1930-12-16 Mcintyre Frederic Metering pump
US2246488A (en) * 1939-08-15 1941-06-17 Detroit Harvester Co Planetary pump
BE536409A (en) * 1953-10-13 1900-01-01
US2879544A (en) * 1955-04-05 1959-03-31 Conte Soc Device for the manufacture of pencils
US3343215A (en) * 1965-04-23 1967-09-26 Barmag Barmer Maschf Deflecting extruder head
US3833704A (en) * 1971-02-24 1974-09-03 Welex Inc Method of extracting a plural layered sheet
DE2252201A1 (en) * 1972-10-25 1974-05-22 5090 Leverkusen DEVICE FOR MANUFACTURING MOLDED PARTS FROM FAST-REACTING CHEMICAL COMPONENTS
GB1601698A (en) 1977-08-20 1981-11-04 Gen Eng Radcliffe Extrusion method and apparatus therefor
US4290989A (en) * 1979-12-10 1981-09-22 Frito-Lay, Inc. Method and apparatus for extruding a plurality of ribbons
US4405547A (en) * 1980-10-20 1983-09-20 The Standard Oil Company Method of coextruding diverse materials
US4356139A (en) * 1980-12-12 1982-10-26 Southwire Company Method for lubricating cable in a dry curing system
US4516922A (en) * 1981-09-29 1985-05-14 At&T Technologies, Inc. Hybrid apparatus for insulating conductors
JPS58128817A (en) * 1982-01-26 1983-08-01 Toppan Printing Co Ltd Manufacturing of modified film
US4413968A (en) * 1982-03-11 1983-11-08 Thiokol Corporation Extrusion die metering device
US4443397A (en) * 1982-08-16 1984-04-17 Cosden Technology, Inc. Multiple-layered sheeting apparatus and process therefor
US4611987A (en) * 1984-07-23 1986-09-16 Cosden Technology, Inc. Apparatus for forming multilayer thermoplastic resin extrusions
FR2593111B1 (en) * 1986-01-17 1988-07-22 Ono THERMOPLASTIC MATERIAL DISTRIBUTION DEVICE FOR THE EXTRUSION OF MULTILAYERED SHEETS.
JPH0655402B2 (en) * 1986-02-19 1994-07-27 東芝機械株式会社 Coextrusion equipment
CH678507A5 (en) * 1986-03-06 1991-09-30 Maillefer Sa
US4786243A (en) * 1986-05-15 1988-11-22 Nabisco Brands, Inc. Apparatus for forming an edible product
GB8623279D0 (en) 1986-09-27 1986-10-29 Lucas Ind Plc Differential gear arrangement
US4761129A (en) * 1987-07-07 1988-08-02 Swisscab E.A. Schoen S.A. Device for changing color during the extrusion of a sheath around a conductor
US4839131A (en) * 1987-09-03 1989-06-13 P.C.E. Corp. Layer width control
US4990293A (en) * 1987-11-09 1991-02-05 Regents Of The University Of Minnesota Process of and apparatus for extruding a reactive polymer mixture
US5190711A (en) * 1988-06-09 1993-03-02 American National Can Company Methods for processing polymers
US5004159A (en) 1988-01-25 1991-04-02 Specified Equipment Systems Company, Inc. Method and apparatus for applying single of multicomponent materials
US4863653A (en) * 1988-02-25 1989-09-05 Idemitsu Petrochemical Co., Ltd. Process of producing thermoplastic resin sheet and equipment therefor
JPH01257022A (en) * 1988-04-08 1989-10-13 Seisan Nipponsha Kk Manufacture of synthetic resin film with rib
US4846658A (en) * 1988-06-20 1989-07-11 Mcmullen Ronald D Extrusion die
DE3821902A1 (en) * 1988-06-29 1990-01-04 Reifenhaeuser Masch PLANT FOR EXTRUDING A MULTILAYERED STRAND OF THERMOPLASTIFIED PLASTICS
US5047196A (en) * 1989-06-29 1991-09-10 Tek-Rap, Inc. Method for forming co-extruded adhesive tapes
US5046938A (en) 1989-11-01 1991-09-10 Hoover Universal, Inc. Improved multiple layer die head with adjustable gaps
JPH03270922A (en) * 1990-03-20 1991-12-03 Bridgestone Corp Fish tail type head of extruder
DE4013553A1 (en) * 1990-04-27 1991-10-31 Hoechst Ag METHOD AND DEVICE FOR THE PRODUCTION OF MOLDED BODIES FROM THERMOTROPES, LIQUID CRYSTALLINE SUBSTANCES AND MOLDED BODIES, MADE BY THE METHOD
DE4025659A1 (en) 1990-08-14 1992-02-20 Leybold Ag CYCLING GEARBOXES WITH ONE WHEEL SET, ESPECIALLY FOR DEVICES FOR COATING SUBSTRATES
JPH04122620A (en) * 1990-09-12 1992-04-23 Mitsubishi Cable Ind Ltd Extrusion molding device for colored electric wire, cable and the like
US5672303A (en) * 1992-10-17 1997-09-30 Bellaform Extrusionstechnik Gmbh Process and extruding head for the manufacture and/or coating of extruding profiles
NL9300572A (en) * 1993-03-31 1994-10-17 Cordis Europ Method for manufacturing an extrusion profile with length-varying properties and catheter manufactured therewith.
US5389324A (en) * 1993-06-07 1995-02-14 The Dow Chemical Company Layer thickness gradient control in multilayer polymeric bodies
US5667818A (en) * 1993-11-05 1997-09-16 Guillemette; A. Roger Extrusion system with balanced flow passage
US5980226A (en) * 1993-11-05 1999-11-09 Guillemette; A. Roger Modular die assembly
US6077062A (en) * 1993-11-05 2000-06-20 Guill Tool & Engineering Co., Inc. Extrusion die system with balanced flow passage
DE4337832C2 (en) * 1993-11-05 1997-07-31 Battenfeld Extrusionstech Process for the production of multilayer products by extrusion or pultrusion
NL9400031A (en) * 1994-01-07 1995-08-01 Cordis Europ Method for manufacturing a tubular extrusion profile and catheter made therefrom.
US5474720A (en) * 1994-03-11 1995-12-12 Friedrich Theysohn Gmbh Method of and apparatus for producing elongated shaped bodies of thermoplastic synthetic resin
JPH08298032A (en) * 1995-04-25 1996-11-12 Nippon Unicar Co Ltd Manufacture of crosslinked polyethylene insulated power cable
DE69520679T2 (en) * 1995-11-10 2001-11-22 Maillefer Nokia Holding Extrusion nozzle with color changing device, for changing the color of the extruded object
GB9604127D0 (en) * 1996-02-27 1996-05-01 Alpha Marathon Mfg Multi-layer blown-film extrusion dye
JP2928789B2 (en) * 1996-04-20 1999-08-03 前田建設工業株式会社 Manufacturing method of layered material
MX9603299A (en) * 1996-08-09 1998-04-30 Serivicios Condumex S A De C V Co-extruded electric conductive cable in three electric method humidity low absorbing isolating layers, low emission toxic gases and vapors, flame retarding.
DE19730993B4 (en) 1997-07-18 2008-04-03 Ald Vacuum Technologies Ag Vacuum coating device for coating substrates on all sides by rotation of the substrates in the particle stream
US6340123B1 (en) * 1997-10-31 2002-01-22 Ching-Chin Lee Universal flow channel
US6130752A (en) * 1998-03-20 2000-10-10 Prisma Fibers, Inc. On-line color monitoring and control system and method
JP2000326384A (en) * 1999-05-24 2000-11-28 Hitachi Cable Ltd Intermittent extruder, intermittent extrusion method and production of catheter
US6447875B1 (en) * 1999-07-30 2002-09-10 3M Innovative Properties Company Polymeric articles having embedded phases
KR100766192B1 (en) * 2000-07-13 2007-10-10 다우 글로벌 테크놀로지스 인크. Tubular Multilayer Films, Method and Apparatus for Preparing the Same
CN1208178C (en) * 2000-09-28 2005-06-29 贝斯托夫有限公司 Screw extruder and gear pump arrangement for highly viscous media
DE10049617B4 (en) 2000-10-05 2005-03-10 Zimmer Ag Device for premixing and feeding additives into a polymer stream
US7367373B2 (en) * 2000-12-06 2008-05-06 Southwire Company Multi-layer extrusion head for self-sealing cable
JP4042096B2 (en) * 2002-04-12 2008-02-06 富士フイルム株式会社 Apparatus and method for manufacturing resin molded product
US6932870B2 (en) 2002-05-03 2005-08-23 Kimberly-Clark Worldwide, Inc. System and process for dispensing an adhesive onto a core during the formation of rolled products
US6676998B2 (en) 2002-05-30 2004-01-13 The Goodyear Tire & Rubber Company Apparatus for continuous coating of wire
US6824733B2 (en) 2002-06-20 2004-11-30 3M Innovative Properties Company Meltblowing apparatus employing planetary gear metering pump
DE10245306B4 (en) * 2002-09-27 2006-03-30 Berstorff Gmbh Extruder / gear pump assembly
ATE484853T1 (en) * 2002-12-02 2010-10-15 Bathium Canada Inc COEXTRUSION PROCESS FOR PRODUCING THIN FILM ELECTROCHEMICAL CELLS FOR LITHIUM POLYMER BATTERIES
US20040251567A1 (en) * 2003-06-13 2004-12-16 Pierluigi Cappellini Method and system for producing plastic optical fiber
DE102004013201A1 (en) * 2004-03-17 2005-10-06 Kuraray Specialities Europe Gmbh Process for the coextrusion of melt streams of different composition
US20060076703A1 (en) * 2004-10-13 2006-04-13 Looman Ernest W Jr Double flow channel for an extruder head
CA2649308A1 (en) * 2006-04-21 2007-11-01 Southwire Company Method and apparatus for multi-stream metered extrusion

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of EP2012911A4 *

Also Published As

Publication number Publication date
US20070246855A1 (en) 2007-10-25
US7754124B2 (en) 2010-07-13
US20100247746A1 (en) 2010-09-30
MX2008013490A (en) 2009-03-25
EP2012911A4 (en) 2014-03-26
US8801987B2 (en) 2014-08-12
WO2007124431A3 (en) 2008-03-27
EP2012911A2 (en) 2009-01-14
CA2649308A1 (en) 2007-11-01

Similar Documents

Publication Publication Date Title
CA2683574C (en) Hybrid hot melt adhesive or other thermoplastic material dispensing system
CN103629452B (en) A kind of method strengthening superhigh molecular weight polyethylene pipe core and steel wire shaping
CA2415277C (en) Tubular multilayer films, method and apparatus for preparing the same
US8801987B2 (en) Method and apparatus for multi-stream metered extrusion
EP0259389B1 (en) Device for supplying plastic material to an extrusion head
JPS6216809B2 (en)
KR20180051369A (en) Systems and methods for additively manufacturing composite parts
KR102064555B1 (en) Manufacturing method and Manufacturing Device pipe opticcable for Telecommunications
US3986477A (en) Wire coating apparatus
CN102596426A (en) Metering system for simultaneously dispensing two different adhesives from a single metering device or applicator onto a common substrate
US4115502A (en) Extrusion method involving rotations
JPS62278514A (en) High power protective cable and manufacture thereof
FI67192C (en) FRUIT PROCEDURE FOR SPRUTNING AV ETT TILLSATSAEMNE IN I HOMOGENISERAD PLAST
US5154865A (en) Process for the production of moldings from thermotropic, liquid-crystalline substances
CN111558505B (en) Optical fiber glue dispensing device and automatic production equipment for flexible netted optical fiber ribbon
KR100788604B1 (en) A Device And A Method For Coating Wire Rod of Optic Overhead Earth Wire
CN104995007B (en) Equipment for producing the electric conductor with least one layer of plastic material coating
CN109291391B (en) Production process of silicon core pipe with information wire
US6550954B1 (en) Method for producing a compound from a flowable plastic material and a solid fiber core by means of extrusion and device for carrying out said method
US6585923B1 (en) Extrusion method and extruder
WO2016086822A1 (en) Metering apparatus and spandex dry spinning component
CN110774560A (en) Flat cable glue injection equipment and flat cable coloring method
CN204370052U (en) Metering device and polyurethane fiber dry spinning parts
CN114433377B (en) Multi-axis spraying device for coating preparation
EP3921854A2 (en) Novelty in the coating and production method of multi-cable pipes

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 07761030

Country of ref document: EP

Kind code of ref document: A2

WWE Wipo information: entry into national phase

Ref document number: 2649308

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: MX/A/2008/013490

Country of ref document: MX

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 2007761030

Country of ref document: EP