EP4045281A1 - Convoyeur de matière fondue pour outil d'extrusion de système d'extrusion, outil d'extrusion, système d'extrusion et procédé d'actionnement de système d'extrusion de ce type - Google Patents

Convoyeur de matière fondue pour outil d'extrusion de système d'extrusion, outil d'extrusion, système d'extrusion et procédé d'actionnement de système d'extrusion de ce type

Info

Publication number
EP4045281A1
EP4045281A1 EP20800002.6A EP20800002A EP4045281A1 EP 4045281 A1 EP4045281 A1 EP 4045281A1 EP 20800002 A EP20800002 A EP 20800002A EP 4045281 A1 EP4045281 A1 EP 4045281A1
Authority
EP
European Patent Office
Prior art keywords
melt
channel
generation
extrusion
channels
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
EP20800002.6A
Other languages
German (de)
English (en)
Inventor
Helmut Meyer
Volkmar KRUK
Tim POHL
Hans-Georg Geus
Anna Klara ROTTSTEGGE
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Reifenhaeuser GmbH and Co KG Maschinenenfabrik
Original Assignee
Reifenhaeuser GmbH and Co KG Maschinenenfabrik
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 Reifenhaeuser GmbH and Co KG Maschinenenfabrik filed Critical Reifenhaeuser GmbH and Co KG Maschinenenfabrik
Publication of EP4045281A1 publication Critical patent/EP4045281A1/fr
Pending legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/30—Extrusion nozzles or dies
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/695—Flow dividers, e.g. breaker plates
    • B29C48/70—Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows
    • B29C48/705—Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows in the die zone, e.g. to create flow homogeneity
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/32—Mixing; Kneading continuous, with mechanical mixing or kneading devices with non-movable mixing or kneading devices
    • B29B7/325—Static mixers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
    • B01F25/4323—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa using elements provided with a plurality of channels or using a plurality of tubes which can either be placed between common spaces or collectors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58—Component parts, details or accessories; Auxiliary operations
    • B29B7/72—Measuring, controlling or regulating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/251—Design of extruder parts, e.g. by modelling based on mathematical theories or experiments
    • B29C48/2511—Design of extruder parts, e.g. by modelling based on mathematical theories or experiments by modelling material flow, e.g. melt interaction with screw and barrel
    • B29C48/2515—Design of extruder parts, e.g. by modelling based on mathematical theories or experiments by modelling material flow, e.g. melt interaction with screw and barrel in the die zone
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/254—Sealing means
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/255—Flow control means, e.g. valves
    • B29C48/2556—Flow control means, e.g. valves provided in or in the proximity of dies
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/256—Exchangeable extruder parts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/362—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using static mixing devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/695—Flow dividers, e.g. breaker plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/92—Measuring, controlling or regulating
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D4/00—Spinnerette packs; Cleaning thereof
    • D01D4/06—Distributing spinning solution or melt to spinning nozzles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/2805—Mixing plastics, polymer material ingredients, monomers or oligomers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92009—Measured parameter
    • B29C2948/92085—Velocity
    • B29C2948/92104—Flow or feed rate
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92009—Measured parameter
    • B29C2948/92209—Temperature
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92323—Location or phase of measurement
    • B29C2948/92361—Extrusion unit
    • B29C2948/92409—Die; Nozzle zone
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92504—Controlled parameter
    • B29C2948/9258—Velocity
    • B29C2948/926—Flow or feed rate
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92504—Controlled parameter
    • B29C2948/92704—Temperature
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92819—Location or phase of control
    • B29C2948/92857—Extrusion unit
    • B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92819—Location or phase of control
    • B29C2948/92857—Extrusion unit
    • B29C2948/92904—Die; Nozzle zone
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92819—Location or phase of control
    • B29C2948/92971—Fluids, e.g. for temperature control or of environment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/695—Flow dividers, e.g. breaker plates
    • B29C48/70—Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows
    • B29C48/71—Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows for layer multiplication

Definitions

  • the invention relates to a fusible link for an extrusion tool of an extrusion plant, comprising a fusible link block with a multi-channel system.
  • the invention also relates to an extrusion tool for at least indirect Extrudie ren or producing extrusion products such as films, nonwovens, profiles, pipes, blow molded parts, filaments, plates, semi-finished products, hoses, cables, compounds or foam semi-finished products.
  • An extrusion tool generally comprises one or more melt conductors, which can be designed as a melt distributor and / or as a melt mixer.
  • the extrusion tool is intended to distribute and / or mix a polymer melt that is held and fed by at least one supply unit and, depending on the design of the melt conductor or melt conductors, to direct it directly into the vicinity of the extrusion tool.
  • one outlet or several outlets of the respective melt conductor functions as an extrusion nozzle or as a nozzle outlet.
  • a separate extrusion nozzle is arranged downstream of the melt conductor or the melt conductor, which is fed with polymer melt from one or more melt conductors and at least indirectly guides the polymer melt from the extrusion tool into the environment.
  • the extrusion tool thus comprises the melt conductor (s) as well as an extrusion nozzle downstream in the direction of flow of the designated polymer melt.
  • the melt conductor (s) and the extrusion nozzle can be separate components. However, it is also conceivable that the melt conductor (s) and the extrusion nozzle are designed in one piece.
  • the extrusion tool can thus be an assembly consisting of the components mentioned and, depending on the design and requirements of the extrusion system, other components.
  • the nozzle outlets of the respective melt conductor or the extrusion nozzle is thus the component forming the extrusion product in the direction of flow of the polymer melt.
  • a melt mixer is to be understood as a component or assembly that receives a plasticized polymer melt in one or more inlets, the polymer melt then being brought together or mixed via merged or intersecting melt channels until the polymer melt is at one or more outlets , the number of which is less than that of the entries from the Schmelzemi shear exits.
  • the polymer melt is therefore initially divided into a large number of melt threads guided in melt channels, which are gradually brought together by the multi-channel system.
  • the melt mixer has melt channels in a direction opposite to the designated flow direction of the polymer melts, which are divided into divided melt channels via at least one branch and several generations of branches. Conversely, melt channels and thus also the melt threads in the designated flow direction of the polymer melts are combined over several generations, so that there are fewer outlets on one outlet side of the melt mixer than there are inlets on an inlet side of the melt mixer.
  • a melt distributor is to be understood as a component or an assembly that receives a plasticized polymer melt in one or more inlets, the polymer melt then being distributed over divided melt channels until the polymer melt at two or more outlets, the number of which is greater than that of the Entrances from the melt distributor, exits.
  • the multichannel system therefore gradually divides the polymer melt into a large number of melt threads guided in melt channels.
  • the melt distributor has melt channels in a designed flow direction of the polymer melt, which channels are divided into divided melt channels over at least one branch and several generations of branches.
  • melt channels are combined in a direction opposite to the designated flow direction of the polymer melt over several generations of merges, so that more outlets are formed on an outlet side of the melt mixer than inlets on an inlet side of the melt mixer.
  • the invention also relates to an extrusion system which is designed in particular as a flat film, meltblown, spunbond, blown film, mono-filament or multi-filament system and comprises an extrusion tool, the extrusion tool having at least one melt conductor of the aforementioned type .
  • the extrusion line is essentially Chen designed to take up an extrudable polymer, to convert it to a polymer melt or to process it further as a polymer melt in order to subsequently produce an extrusion product through a suitable line of the polymer melt and downstream atomization.
  • extruable polymer essentially means materials and their mixtures and commercially available additives that can be extruded or processed by an extruder.
  • the polymer can be a plastic polymer.
  • thermoplastic starch solutions and other materials can also be extruded and can be used for the present invention instead of or together with a plastic polymer.
  • present patent application usually only speaks of “polymer” or “plastic polymer”.
  • the extrudable polymer can be provided to the extrusion system, for example, as granules or powder or flakes in essentially solid form. Alternatively, it is conceivable that at least part of the extrudable polymer is in essentially liquid form.
  • the supply unit which holds the extrudable polymer can be, for example, a reservoir which provides the polymer for feeding the melt conductor in the form suitable for the melt conductor.
  • the supply unit can be an extruder which converts the extrudable polymer beforehand into a phase which is optimal for feeding the melt conductor, for example from an essentially solid form to an essentially liquid form.
  • the polymer melt When the melt conductor is fed, the polymer melt is generally essentially completely melted or plasticized or in solution and is then divided up and / or brought together by the melt conductor. It is also possible that part of the polymer is in essentially solid form or is added to the essentially liquid or melted polymer melt as an additive or additive before the melt conductor is fed, the solid portion may have a different melting temperature than the one - melted proportion. In other words, the polymer in this case consists of at least two components which are fed to the fusible conductor together or separately.
  • the invention also relates to a method for operating an extrusion plant.
  • extrusion tools with a circular or annular gap-shaped exit cross-section on the extrusion nozzle there are spiral distributors for charging round nozzles with polymer melt provided from a supply unit, the spiral distributors having spiral grooves which are incorporated on the outside or inside of a jacket surface of a mandrel or a quill.
  • pin distributors or bar dome holders also exist, by means of which polymer melt can be distributed evenly in such a way that a film tube or a profile can emerge from the extrusion tool.
  • extrusion tools with a slot-shaped exit cross section on the extrusion nozzle are known.
  • the aim of the melt conductor of this extrusion tool is to convey a polymer melt provided by a supply unit as evenly as possible to the nozzle outlets or the extrusion nozzle, so that a required amount of polymer melt is present over a desired width at every point of the nozzle outlet.
  • a polymer melt provided by a supply unit as evenly as possible to the nozzle outlets or the extrusion nozzle, so that a required amount of polymer melt is present over a desired width at every point of the nozzle outlet.
  • Fusible line systems as T-distributors, fishtail distributors and clothes hanger distributors.
  • extrusion tools with a large number of individual outlet cross-sections are known.
  • the aim of the melt conductor of this extrusion tool is to feed a polymer melt provided by a supply unit as uniformly as possible to the nozzle outlets or the extrusion nozzle.
  • these melt conductors are designed as T-distributors, clothes hanger distributors, strand distributors, channel distributors, step distributors, pin distributors, spiral distributors or gap distributors.
  • melt conductors are used to uniformly distribute or merge a polymer melt, which is essentially continuously provided by a provision unit, from an inlet side of the melt conductor with a total inlet cross-sectional area to an outlet side of the melt conductor with a geometrically and spatially significantly changed total outlet cross-sectional area than the total inlet cross-sectional area.
  • a melt conductor designed as a melt distributor has the task of providing the polymer melt downstream on the outlet side of the melt distributor with a larger total outlet cross-sectional area than was fed to the melt conductor upstream.
  • the polymer melt must be distributed evenly from a first overall passage cross-section to a second overall passage cross-section with a greater width, whereby the respective melt channel cross-section exiting on the outlet side does not have to run in a straight line, as is the case with a slot nozzle arranged on the outlet side, but also in a curved or curved shape circular, for example with regard to a round nozzle arranged on the outlet side.
  • the total circumference of the second total passage cross-section that is to say the sum of all the circumferences of the melt channels on the outlet side of the melt conductor, is significantly greater than that of the first total passage cross section on the inlet side of the melt conductor.
  • a melt conductor designed as a melt mixer has the task of providing the polymer melt downstream on the outlet side with a smaller overall outlet cross-sectional area than was fed to the melt conductor upstream.
  • the polymer melt has to move uniformly from a first total passage cross-section to a total passage cross-section with a significantly smaller one Total cross-sectional area are brought together or mixed, with the respective melt channel cross-section emerging on the outlet side not having to run in a straight line in this case either.
  • the polymer melt is generally provided continuously on the inlet side of the melt conductor by at least one supply unit, in particular by at least one extruder or the like, and fed to the melt conductor.
  • the polymer melt is at least indirectly atomized in order to continuously produce an extrusion product.
  • DE 21 14 465 A discloses a device for evenly distributing thermoplastic plastics from at least one extruder head nozzle to several blow or pointed heads, the device having a massive manifold block in which a large number of bores and additional bolts are introduced in order to create melt lines as well as diversion points within the massive distributor block.
  • EP 0 197 181 B1 describes a method for producing a composite injection molding distributor, the injection molding distributor having various branches in order to transfer melt from a common inlet opening to a plurality of outlet openings.
  • the injection molding manifold is screwed together from two plates made of tool steel with opposing surfaces, the surfaces having matching grooves in order to design melt channels in the interior of the melt manifold.
  • melt distributor for plasticized plastic melt in an extruder is known, which after being pressed out of an extrusion nozzle is divided into several individual strands for individual processing tools.
  • the melt distributor has a feed channel and an adjoining nozzle with distributor channels, the number of distributor channels corresponding to the number of processing tools, and the center points of the mouths of the distributor channels formed on the nozzle lie on a circle in order to melt plastic on all processing tools as much as possible to be able to provide the same temperature profiles.
  • a fusible link of an extrusion system should be thought of, which either itself has nozzle outlets for producing extrusion products or is designed to feed a shaping extrusion nozzle. So let us think of such a fusible link that is part of an extrusion tool of an extrusion plant.
  • the phrase “for an extrusion tool of an extrusion system” should not imply that the extrusion tool or the system should be a mandatory part of the respective claim, but rather only require suitability.
  • the wording “for an extrusion system” should not imply that the system should be a mandatory part of the respective claim.
  • the invention is based on the object of further developing fusible conductors and overcoming their disadvantages.
  • the invention is based on the object of further developing extrusion tools, extrusion systems and related processes, in particular for operating such extrusion systems.
  • this object is achieved by a fusible link with the features of independent claim 1.
  • Advantageous further developments of the fusible conductor emerge from the subclaims 2 to 12.
  • the object of the invention is achieved by an extrusion tool according to claim 13.
  • Advantageous further developments of the extrusion tool emerge from dependent claim 14.
  • the object of the invention is achieved by an extrusion system according to patent claim 15.
  • the object of the invention is achieved by a method for operating such a system according to patent claim 16.
  • a melt conductor for an extrusion tool of an extrusion plant, having a melt conductor block with a multi-channel system, the multi-channel system being arranged in a three-dimensional manner within the melt conductor block and at least one inlet and at least has an outlet for polymer melt, whereby between an inlet and an outlet fluidically connected to the inlet, several branches arranged one behind the other and several generations of further branches are formed over several generations of divided melt channels, m melt channels of the a-th generation with x-th local cross-sections and n melt channels of the b-th generation y-th local cross-sections are present, where n> m, if b> a, where the y-th local cross-sections of the melt channels of the b-th generation are smaller than the x-th local cross-sections of the melt channels of the a-th generation, and where in In the designated flow direction of
  • a “fuse link” is a component or an assembly comprising a fuse block with the multi-channel system, which is designed to distribute and / or merge a polymer melt fed to the fuse link, depending on the design of the multi-channel system.
  • the melt conductor can be designed exclusively as a melt distributor, which distributes the designated polymer melt from at least one inlet to a large number of outlets.
  • the melt conductor can be designed exclusively as a melt mixer which brings together the designated polymer melt from two or more inlets to one of the total number of outlets that is lower than the number of inlets.
  • the melt conductor can be designed in any order partly as a melt distributor and partly as a melt mixer, so that the designated polymer melt can be distributed and combined as desired, the number of inlets and outlets being selectable as required according to the application.
  • the melting conductor is preferably produced at least partially by means of an additive manufacturing process.
  • the “fuse block” is the name given to that component of the fuse element that completely or partially accommodates the multi-channel system.
  • the fusible conductor block is preferably formed by means of an additive manufacturing process.
  • the fusible terblock can be a base body which is solid or with support structures, for example, is designed in a skeleton construction.
  • the support structures can be formed to ensure static stability of the fusible conductor block, wherein the support structure can also be formed to support the multi-channel system.
  • the melt conductor is designed as a melt distributor, the term “melt distributor block” is used as a synonym for the melt conductor block.
  • the melt conductor is designed as a melt mixer, the term “melt mixer block” is used as a synonym for the melt conductor block.
  • a plurality of fusible conductor blocks can be provided, which are arranged in a stationary manner with respect to one another and form the fusible conductor in a modular manner, with the individual fusible conductor blocks thus preferably being exchangeable are designed and arranged to one another in such a way that simple assembly, maintenance and / or servicing of the fuse element is possible.
  • the fusible conductor blocks can be connected to one another in a releasable manner, that is to say for example by means of mutual bracing, but also in a non-releasable manner, that is to say in particular with a material fit.
  • a releasable connection or bracing is understood to mean that the individual fusible conductor blocks are designed to be non-destructive or replaceable, for example in the event of damage, for maintenance measures, for transport or the like.
  • a “melt channel” denotes a polymer melt or a melt stream of the polymer melt, which is essentially elongated section of the multichannel system and which extends exclusively longitudinally or straight or can have curvatures, for example in the form of curves, around a three-dimensional configuration of the multi-channel system.
  • a plurality of such melt channels are fluidically connected to one another via branches and further branches and thus form the multi-channel system, whereby two or more melt channels can be arranged in series and / or in parallel in order to distribute and / or mix the polymer melt according to the requirements of the melt conductor .
  • the melt channels extend from the respective inlet to the respective outlet fluidically connected to the inlet.
  • the respective melt channel can be shaped as desired. It is thus conceivable that the melt channel has an essentially unchanged melt channel cross-section, that is to say a local cross-section of any configuration which extends over the entire length of the respective melt channel between the branches.
  • the local cross-section can have an essentially circular cross-sectional shape, an essentially oval or elliptical cross-sectional shape and / or an essentially rectangular or square cross-sectional shape.
  • a cross-sectional shape that deviates from the known geometric standard shapes can also be selected for the melt channel, in particular in the case of transitions between the known standard shapes.
  • the respective melt channel has the said cross-sectional shape or the local cross-section essentially constant over a large part of its axial extent, preferably greater than or equal to 50 % the length of the respective melt channel, preferably of at least 2/3 the length of the respective melt channel, furthermore preferably of at least 3/4 of the length of the respective melt channel.
  • the “designated flow direction” of the polymer melt relates to the arrangement of the melt conductor in the extrusion system as well as the design of the multi-channel system, whereby the flow direction always runs from an inlet to an outlet fluidically connected to the inlet, regardless of whether the polymer melt is distributed in the multi-channel system and / or mixed.
  • the designated flow direction of the polymer melt runs from an entry side to an exit side of the melt conductor.
  • a “multichannel system” is a channel structure within the fuse link, preferably at least partially produced by means of an additive manufacturing process, which is integrated in the fuse block and extends three-dimensionally within the fuse block.
  • the multi-channel system consists of a large number of melt channels fluidly connected to one another, which extend from at least one inlet to at least one outlet fluidly connected to the inlet and which, depending on the design of the melt conductor, are fluidically connected to one another via branches and further branches or via merges.
  • the melt channels of the multi-channel system are fluidically connected in series or arranged in parallel to one another.
  • At least one a-th generation melt channel When connected in series, at least one a-th generation melt channel is fluidically connected via a branching or branching with at least one b-th generation melt channel, the a-th generation melt channel depending on the design of the melt conductor as a distributor or mixer in the designated flow direction of the Polymer melt downstream or upstream of the respective b-th generation melt channel.
  • the a-th generation melt channel is via a branch or a junction fluidically connected to the bth generation melt channel.
  • several, preferably all, melt channels of a respective generation are arranged in parallel.
  • An “entry” of the multichannel system is to be understood as the entry of the multichannel system into the fusible link block, into which the polymer melt provided by a supply unit is fed into the fusible link block.
  • the respective inlet is arranged on the inlet side or on an inlet side on the fusible conductor block.
  • an “exit” of the multichannel system is to be understood as the exit or outflow of the multichannel system from the fusible link block from which the polymer melt guided or distributed and / or merged through the fusible link block emerges from the fusible link block.
  • the respective outlet can be designed in such a way that it functions as a nozzle, the respective outlet thus being a nozzle outlet.
  • the respective outlet can also be designed such that it feeds an extrusion nozzle connected downstream of the melt conductor, which atomizes the polymer melt accordingly in order to produce an extrusion product at least indirectly.
  • the respective outlet is therefore arranged on the outlet side or on an outlet side on the fusible conductor block.
  • the fusible conductor block accordingly has an inlet side and an outlet side, the inlet side with the respective inlet being arranged downstream of the supply unit in relation to the designated flow direction of a polymer melt, and the outlet side with the respective outlet upstream of an extrusion nozzle or downstream of the inlet side is arranged with the respective entry.
  • the melt conductor has more outlets than inlets, since the respective inlet is preferably fluidically connected to a plurality of outlets over at least two generations of divided melt channels.
  • a total cross-section of all local cross-sections of the melt channels of a respective generation increases with increasing generation.
  • the respective local transverse Cross-section of the n melt channels of the bth generation compared to the respective local cross-section of the m melt channels of the a-th generation, but the number of melt channels increases from generation to generation, i.e. with increasing alphabetical order.
  • the a-th generation melt channel is oriented towards the entry, the b-th generation melt channel being oriented toward the exit and following the a-th generation melt channel in the designated flow direction of the polymer melt. Accordingly, a c-th generation melt channel follows the b-th generation melt channel in the designated flow direction of the polymer melt, and so on, with the c-th generation melt channel also exiting in relation to the a-th and b-th generation melt channel is too oriented.
  • the melt channel of the b-th generation is to be oriented towards the entrance in relation to the melt channel of the c-th generation.
  • a melt channel of an a-th generation is divided into at least two melt channels of a fi th generation, with a melt channel of the b-th generation in turn being divided into at least two melt channels of a c-th generation, and so on.
  • the alphabetical series of the generations of the melt channels and the number of melt channels along the designated flow direction of the polymer melt increases from generation to generation.
  • the melt conductor has more inlets than outlets, since at least two of the inlets are fluidically connected via preferably at least two generations of merged melt channels with a smaller number of outlets.
  • the total cross-section of all local cross-sections of the melt channels of a respective generation decreases with decreasing generation in order to prevent a melt flow of the designated polymer melt and to keep the wall shear stresses in the multi-channel system essentially constant.
  • the respective local cross-section of the n melt channels of the bth generation increases compared to the respective local cross-section of the m melt channels of the a-th generation, the number of melt channels decreases from generation to generation, i.e. with a decreasing order of the alphabet.
  • the respective c-th generation melt channel is oriented towards the inlet, the b-th generation melt channel being oriented towards the outlet and in the designated flow direction of the polymer melt towards the c-th generation melt channel follows. Accordingly, a melt channel of the a-th generation follows in the designated flow direction of the polymer melt on the b-th generation melt channel, and is also oriented towards the outlet in relation to the c-th and b-th generation melt channel. In contrast, the melt channel of the bth generation is oriented towards the entrance in relation to the melt channel of the cth generation.
  • melt conductor partially as a melt conductor and partially as a melt mixer.
  • this is to be understood as meaning that a melt channel of an a-th generation is initially divided into at least two melt channels of a b-th generation, with a melt channel of the b-th generation in turn dividing into at least two melt channels of a c-th generation so that the polymer melt is initially distributed from generation to generation.
  • At least two melt channels of the c-th generation can subsequently be merged again into a smaller number of melt channels of a b'th generation, with at least two melt channels of the b'th generation subsequently being able to be merged into melt channels of the a'-th generation, and so on, so that the polymer melt is merged from generation to generation.
  • a reverse arrangement in which melt channels are first brought together and then divided, as well as any combination of distributions and merges, is also conceivable, depending on the requirements for the polymer melt and the extrusion product made from it.
  • the wording “to be oriented” is to be understood in the context of the invention as an arrangement of a melt channel and / or a branching or further branching of a first generation relative to a further generation. If a multichannel system has, for example, an a-th, b-th and c-th generation melt channels, with the a-th generation directly at the entry of the fusible link block, the c-th generation directly at the exit of the fusible link block and the b-th generation in designated flow direction of the polymer melt are arranged between the a-th and c-th generation, then the Melt channel of the a-th generation relative to the melt channels b-th and c-th generation oriented towards the entrance.
  • melt channel of the c-th generation is oriented towards the outlet relative to the melt channels of the a-th and b-th generation.
  • the melt channel of the bth generation is consequently on the one hand to be oriented relative to the melt channel of the a-th generation at the exit and on the other hand to be oriented relative to the melt channel of the cth generation at the entrance.
  • the term “three-dimensionally extending” is to be understood as meaning that the multi-channel system can be designed or shaped in up to six different degrees of freedom within the melt conductor block.
  • a melt channel of the multichannel system can run vertically upwards and / or downwards and / or horizontally to the left and / or to the right and / or forwards and / or backwards in sections. Regardless of how the multi-channel system is designed within the fusible link block, at least three of the six degrees of freedom are always used.
  • a vertically downward-running melt channel of a-th generation is divided into two melt channels of b-th generation via a substantially 90 ° branch in a common plane
  • the divided melt channels run, for example, in a horizontal direction starting from the melt channel of a-th generation to the left or right.
  • three degrees of freedom are already used.
  • one of the melt channels is branched in such a way that at least one of the divided melt channels runs partially at an angle to said plane, a fourth and / or fifth degree of freedom is used.
  • one of the bth generation melt channels can also be partially directed opposite to the a-th generation melt channel, which is directed vertically downwards, that is, with an opposite flow direction of the polymer melt, so that the sixth degree of freedom is also used.
  • a curved design of the multi-channel system or the melt channels and / or the further branches in space is conceivable, so that several degrees of freedom can be used at the same time.
  • a “branch” or “further branching” is a junction at which a melt channel is divided into at least two melt channels regardless of a flow direction of a polymer melt.
  • a further branch is a branch from the second generation.
  • a melt channel of the last generation is branched into two or more melt channels.
  • bth generation ze channels divided.
  • a b-th generation melt channel is subsequently divided into two or more c-th generation melt channels via a further branching.
  • the branch or branches each function as a junction, with two or more melt channels of the bth generation being merged or combined via a junction into a melt channel of the a th generation or a smaller number of melt channels of the a th generation become.
  • melt conductor designed as a melt distributor
  • the multi-channel system is therefore preferably designed in such a way that the polymer melt always has the same, that is, a symmetrical melt history. This also makes it possible for the polymer melt to be distributed particularly uniformly over the area on the outlet side of the melt distribution block and thus also to be provided particularly uniformly in an extrusion space adjoining these outlet channels further downstream, i.e. in particular a collecting space and / or an inlet of the extrusion nozzle.
  • the term “equal shear stresses” essentially describes wall shear stresses between the wall of the multi-channel system and the polymer melt conducted in the respective melt channel, in particular in all branching stages or in all generations of the melt channels, the shear stresses being essentially the same or constant or are approximately the same or constant, with the shear stresses deviating from one another by less than 30%, preferably less than 20% and particularly preferably less than f0%.
  • the multichannel system is preferably designed in such a way that the polymer melt exits always has the same, that is, a symmetrical history. This also makes it possible for the polymer melt to be brought together particularly evenly on the outlet side of the fusible conductor block and thus also be provided in a targeted manner in an extrusion space adjoining the outlet duct or ducts further downstream, i.e. in particular a collecting space and / or an inlet of the extrusion nozzle.
  • each melt channel of a respective generation decreases with increasing generation as well as in the designated flow direction of the polymer melt, whereby the sum of melt channels per generation increases with increasing generation, so that a division of melt flows takes place from generation to generation in the designated flow direction.
  • each melt channel of a respective generation increases with decreasing generation and in the designated flow direction of the polymer melt, whereby the sum of melt channels per generation decreases with decreasing generation, so that from generation to generation a merging of melt flows takes place in the designated flow direction.
  • a "means for at least indirect influencing of the polymer melt” is to be understood as a device, an assembly, a component and / or an element which directly or indirectly influences, i.e. manipulates and / or changes the melt flow conducted in a respective melt channel of the multi-channel system.
  • the term “at least indirectly” also means that the means for influencing the polymer melt and the polymer melt conducted in the respective melt channel of the multi-channel system via a further component or functional element, which is arranged between the means for influencing and the polymer melt, with one another Are (effectively) connected or are connected to one another directly and thus directly or without an intervening component.
  • a thermally conductive material can be arranged, the means for influencing thus a device for temperature control of the polymer melt is. This results in an indirect or indirect influence on the polymer melt, the flow properties of which are improved by the influence of heat.
  • components or elements can be provided on or in the melt channel which mix, accelerate and / or slow down the melt flow conducted in the respective melt channel, for example ramps, struts, perforated disks, channels, static or variable cross-section modifiers, or the like.
  • This results in a direct or direct influencing of the polymer melt since the influencing means arranged in or on the respective melt channel come into direct contact with the polymer melt.
  • the respective means for at least indirectly influencing the polymer melt can be formed by means of an additive manufacturing process, specifically separately or in the course of manufacturing the fusible conductor block, in particular the multi-channel system.
  • a means for at least indirectly influencing the polymer melt is preferably a static functional element, an actuator, a bimetal, a part movably arranged in a melt channel, a pump, an exchangeable plug-in element and / or a cross-section changer for the multi-channel system.
  • a “static functional element” is to be understood as meaning at least one essentially stationary element or component which is arranged or formed on or in the multichannel system and interacts with the designated polymer melt.
  • the static functional element implements such an influence on the designated polymer melt, so that the properties, in particular the flow properties, of the polymer melt remain essentially the same from entry to exit, and are preferably improved.
  • the static functional element can have the effect that a melt temperature of the melt flow is made more homogeneous. Deposits and / or segregation phenomena of the polymer melt in the multi-channel system can also be prevented by homogenizing the melt flow.
  • an “actuator” is to be understood as an electromechanical drive element which influences the melt flow at least indirectly, preferably directly or directly.
  • the actuator can be arranged on or in the respective melt channel and mechanically influence the polymer melt guided on it. In particular, the actuator can do this can be used to influence the amount of polymer across the width B of an extrusion nozzle outlet of an extrusion nozzle.
  • a “bimetal” within the meaning of this invention is a component that is operatively connected to the respective melt channel or part of the fusible conductor block that is operatively connected to the respective melt channel and consists of two different metals that are connected to one another in a material and / or form-fitting manner.
  • the bimetal can, for example, have two superimposed layers with different metals. Due to the different coefficients of thermal expansion of the metals used, one of the layers expands more than the other when exposed to heat, causing the bimetal to deform locally, for example. These material properties can be used to realize a local deformation of the local cross-section of the respective melt channel. A temperature-dependent local expansion or local tapering is therefore possible.
  • the bimetal can preferably also be produced additively during the production of the fusible conductor block or the multichannel system.
  • the bimetal is preferably designed to locally change a channel geometry of at least one of the melt channels as a function of a preferably electrically and / or fluidically induced temperature change on the fusible conductor block.
  • a part that is movably arranged in the respective melt channel is an element or component that is arranged in or on the melt channel in such a way that it either actively influences the polymer melt through a dynamic movement or is actuated by the polymer melt in such a way that it influences the polymer melt.
  • kinetic energy of the flowing polymer melt can be transferred to the part movably arranged in the respective melt channel.
  • the movably arranged part is arranged around an axis of rotation, for example.
  • the part movably arranged in the respective melt channel can be, for example, a wheel, a turbine blade and / or a flap that influences the polymer melt in such a way that the flow rate and the material properties of the melt stream are homogenized.
  • the axis of rotation of the movably arranged part can, depending on the design and arrangement of the movably arranged part, run coaxially, parallel or obliquely to the longitudinal direction of the respective melt channel. It is alternative or complementary It is conceivable that such a part is also movably arranged in the area or within a branch or a further branch.
  • a means designed as a “pump” for at least indirect influencing of the polymer melt is to be understood as a conveying means for polymer melt which realizes an energy transfer to the polymer melt by fluid mechanical processes. A change in pressure and / or flow rate is therefore made possible by the pump arranged in or on the respective melt channel.
  • an “exchangeable plug-in element” is a component which can at least partially be inserted into the melt distribution block and which, after being inserted into the melt distribution block, influences the polymer melt.
  • the plug-in element can be designed in the form of a cassette and can be inserted and fixed in a complementary recess on the melt distribution block.
  • the plug-in element can comprise one or more of the aforementioned means for influencing the polymer melt.
  • a “cross section changer” is an element which is arranged in or on the respective melt channel and which locally changes the cross section of the respective melt channel.
  • the cross-section changer changes a flow rate locally, and this can be done statically or dynamically. This can take place in the form of a lip formed in the melt channel, ie statically or dynamically, for example in the form of a valve that sets a flow rate through the respective melt channel or adapts it to the requirements.
  • the exchangeable plug-in element is preferably designed to locally change a channel geometry of at least one of the melt channels and / or to fluidically connect at least two of the melt channels of the multi-channel system to one another.
  • the plug-in element can have melt channel sections and / or branches in order to realize a local merging or division of melt channels.
  • the local cross section of the melt channel sections can alternatively or additionally be larger or smaller than the respective melt channel to which the plug-in element is operatively connected.
  • a cross-sectional shape of the melt channel of the respective generation can be locally changed, namely enlarged or reduced.
  • the plug-in element can also be designed to change the geometry and design of the multi-channel system over several generations of melt channels and / or over several generations of branches and further branches.
  • the plug-in element can also be designed to change the geometry and design of the multi-channel system over several generations of melt channels and / or over several generations of branches and further branches.
  • the fusible conductor in particular the fusible conductor block, preferably has an inspection opening with an external access to the multi-channel system.
  • the multi-channel system can be checked for possible blockages or deposits through an inspection opening.
  • a rinsing or cleaning process of the multi-channel system can be carried out or supported via the inspection opening.
  • the revision opening is designed to be closable, so that an unintentional influencing of the polymer melt via the revision opening is prevented during the operation of the extrusion system.
  • Melt ladder in particular melt distributor or melt mixer, for an extrusion tool of an extrusion system, having a melt conductor block with a multichannel system, the multichannel system extending three-dimensionally within the fusible conductor block, the melt ladder, in particular the melt ladder block, having an inspection opening to the multichannel system.
  • the fusible conductor in particular the fusible conductor block, preferably has a valve receptacle with an external access to the multichannel system.
  • the external access can be a separate access or integrated in the inspection opening.
  • the valve receptacle is arranged on the respective melt channel and can be designed as a cavity for receiving a valve.
  • the valve receptacle can be designed in such a way that a filter device can be accommodated in order, for example, to filter suspended particles from the polymer melt.
  • the filter device can in turn comprise a filter element which is accessible and removable via the external access or the inspection opening.
  • Melt ladder in particular melt distributor or melt mixer, for an extrusion tool of an extrusion plant, having a fusible conductor block with a multichannel system, the multichannel system extending three-dimensionally within the fusible conductor block, the fusible conductor, in particular the melt ladder block, a valve receptacle with an external access to the Multi-channel system has.
  • the fusible conductor in particular the fusible conductor block, has a through opening with an external access to the multi-channel system, by means of which a medium can be guided to the multi-channel system and / or away from the multi-channel system.
  • the passage opening can be a separate channel to a respective melt channel or part of the inspection opening.
  • the through opening can be a separate channel system for access to a plurality of melt channels of one generation or of different generations.
  • the medium can be a liquid or a gas, wherein the liquid can also have a solid content.
  • the passage opening is optionally designed to derive air from the multi-channel system or to add it to the multi-channel system.
  • the through-opening is therefore designed for ventilating and / or venting the multi-channel system.
  • the through opening for adding an additive is formed in at least one melt channel of the multi-channel system. It is therefore conceivable that the The passage opening is part of the inspection opening.
  • the addition of an additive via the respective passage opening is particularly relevant in what is known as compounding, with at least one additive being added to the polymer melt for the production of the extrusion product.
  • An additive is advantageous in order to adjust the material properties of the finished plastic to the requirements of the respective application or to influence the material properties of the polymer melt during processing.
  • additives in the plastic sometimes improve the chemical, mechanical and / or electrical properties of the compound in question. Additives are, in particular, plasticizers, stabilizers, reinforcing agents, colorants or fillers, as well as propellants or lubricants.
  • Melt ladder for an extrusion tool of an extrusion system, comprising a melt conductor block with a multichannel system, the multichannel system extending three-dimensionally within the fusible conductor block, wherein the fusible conductor, in particular the melt conductor block, has a through opening with an external access to the Has multichannel system, by means of which a medium can be guided to the multichannel system and / or away from the multichannel system
  • a means for at least indirect influencing of the polymer melt is preferably a manipulation device which can be selected and alternately activated and deactivated for manipulating melt areas arranged within the fusible conductor block and set up for guiding polymer melt.
  • Melt areas are all sections of the multichannel system that carry the polymer melt, thus the respective entry, the melt channels of all generations, all branches and further branches, as well as the respective exit.
  • the manipulation device can be switched on or off depending on the operating situation of the extrusion system. It can therefore be verbun with a control unit or a computer unit which initiates and carries out activation or deactivation.
  • a control unit or a computer unit which initiates and carries out activation or deactivation.
  • each manipulation device is only operatively connected to individual melt areas or segments of the melt conductor block.
  • Melt ladder in particular melt distributor or melt mixer, for an extrusion tool of an extrusion plant, comprising a melt conductor block with a multichannel system, the multichannel system being arranged in a three-dimensional manner within the fusible conductor block, the fusible conductor, in particular the melt ladder block, being selectively and alternately activatable has deactivatable Manipulationsein direction for manipulating melt areas arranged within the fusible conductor block for guiding polymer melt.
  • the manipulation device is designed to be temperature-controlled.
  • the manipulation device comprises a temperature control element and / or a temperature control strip, wherein the temperature control element or the temperature control strip can be arranged in or on the corresponding melt area.
  • the temperature control element or the temperature control strip is advantageously designed to temperature control a material that surrounds and forms the multichannel system, which in turn influences the temperature of the polymer melt within the multichannel system. flows.
  • the temperature control element can influence the polymer melt locally, whereas the temperature control strip can be arranged, for example, circumferentially around the respective melt channel and / or along its longitudinal extension in order to influence the polymer melt temperature accordingly.
  • Melt ladder in particular melt distributor or melt mixer, for an extrusion tool of an extrusion plant, having a melt conductor block with a multichannel system, the multichannel system extending three-dimensionally within the melt ladder block, the melt ladder, in particular the melt ladder block, being a temperature-controlled, selectable and alternating activatable and deactivatable face manipulation device for manipulating melt areas arranged within the fusible conductor block for guiding polymer melt.
  • the fusible conductor block preferably also has a media channel, in particular for a circulating fluid supply, especially for temperature control and / or for an electrical line and / or for a measuring device.
  • a “media channel” is to be understood as an additional channel system that is formed in addition to the multi-channel system and fluidically separated therefrom, and which can basically be designed like the multi-channel system in terms of structure.
  • the media channel can also extend three-dimensionally through the melt conductor block and has an inlet and an outlet fluidically connected to it.
  • the media channel runs spatially spaced between the melt channels of the multichannel system and can be operatively connected to the multichannel system.
  • the media channel can be designed, for example, to guide a medium, in particular a temperature control medium.
  • the media channel is a separate, space-saving channel or a separate channel system. system through which an interaction with the designated polymer melt guided in the melt channels can be realized.
  • the media channel or another media channel for guiding electrical lines and / or a measuring device can be provided. Due to its additive manufacturing, the multi-channel system can be routed around the media channel, which can also be additively manufactured, or vice versa.
  • the support structures described above can also be used to achieve static stability of the median canal.
  • Melt ladder in particular melt distributor or melt mixer, for an extrusion tool of an extrusion plant, having a melt conductor block with a multichannel system, the multichannel system extending three-dimensionally within the melt conductor block, the melt conductor, in particular the melt conductor block, being arranged spatially between melt channels of the multichannel system Has media channel, in particular for a circulating fluid supply, especially for temperature control, and / or for an electrical line and / or for a measuring device.
  • the static functional element is a static mixing element.
  • the static mixing element is preferably arranged within the multichannel system or in a melt channel of the multichannel system and is advantageously also at least partially additively manufactured in the case of additive manufacturing of the multichannel system.
  • the mixing element can be ramp-shaped, rod-shaped, curved or the like and is used primarily for mixing and homogenizing the designated polymer melt. Due to the existing shear stresses in the polymer melt, there are different flow velocities of the melt flow in the melt channel, which flow speeds decrease from a central axis of the melt channel towards the melt channel wall.
  • the static functional element in particular the static mixing element, realizes in this context an equalization of the flow in the melt channel. th melt strand. For example, immediately before the exit of the multi-channel system, a uniformity of the melt flow by a static mixing element can realize a uniform supply of an extrusion nozzle or a collecting space formed upstream of the extrusion nozzle.
  • the static mixing element is preferably arranged in the melt channel between two branches or further branches. It is conceivable that a slight local change in cross-section of the local cross-sectional shape of the melt channel is formed in the area of the mixing element, in particular in order to improve a mixing effect.
  • a local widening of the melt channel is preferably provided, which is shaped as a function of the flow properties present in the respective melt channel, the static mixer being formed within the local widening.
  • the melt channel preferably has essentially the same cross-sectional size and shape before and after the local widening of the melt channel, a locally enlarged cross-section being formed in between in the designated flow direction of the polymer melt.
  • the change in cross-section can be step-shaped and / or ramp-shaped. Furthermore, it is advantageous if, after a change in direction of the melt channel, the polymer melt or the melt flow is directed from the central axis of the respective melt channel in the direction of the wall of the melt channel using a simple static mixing element.
  • melt ladder in particular melt distributor or melt mixer, for an extrusion tool of an extrusion plant, comprising a melt conductor block with a multichannel system, the multichannel system extending three-dimensionally within the melt conductor block, the melt conductor, in particular the melt conductor block, having a static mixing element.
  • the invention includes the technical teaching that the fusible conductor block has a first multi-channel system and a second multi-channel system, in particular a third, fourth or fifth multi-channel system. It is conceivable that the multi-channel systems run fluidically separated from one another or that at least two multi-channel systems are brought together in order to mix the polymer melts of the combined multi-channel systems with one another.
  • multi-channel systems are also conceivable, each of which is at least partially formed by means of an additive manufacturing process within the melt conductor block.
  • the multichannel systems can conduct identical, but for example also different or partly identical and partly different polymer melts in order to produce, for example, multi-layer or at least partly overlapping film webs or filaments.
  • Polymer melts that differ in terms of their material requirements and properties can also be conducted, in particular brought together and / or distributed in the multi-channel systems, in order to produce a corresponding extrusion product.
  • individual filaments are produced from polymer melts from various multi-channel systems. Filaments can therefore be formed from different components or polymer melts with any mixing ratios, the components being arranged, for example, adjacent to one another, in layers, layers and / or segments in the respective filament.
  • Nonwovens or nonwovens with the same or different material properties can be produced from a large number of filaments.
  • a fleece consists of a large number of individual filaments, preferably from 20 to 10,000 individual filaments per meter of width of the fleece.
  • the outlets of the respective multi-channel system can be designed to atomize the polymer melt to form a filament. It is also conceivable that the extrusion nozzle downstream of the fusible conductor block is provided for producing the filaments and then the fleece.
  • an extrusion tool for an extrusion system for producing extrusion products comprising a melt conductor according to the type described above, the melt conductor being designed to distribute and / or mix at least one polymer melt.
  • An “extrusion tool” is to be understood as an assembly of an extrusion system that has one or more fusible links with one or more fusible link blocks each includes.
  • the extrusion tool is fed with polymer melt, which is passed at least indirectly into the melt conductor or a multi-channel system of a melt conductor block of the melt conductor.
  • a supply unit in the form of an extruder or the like for supplying the designated polymer melt is arranged upstream of the extrusion tool.
  • At least one extrusion nozzle which can also be part of the extrusion tool, is preferably arranged downstream of the melt conductor or the respective melt conductor block.
  • the extrusion nozzle in turn has an extrusion nozzle outlet which is designed for intermediate shaping or final shaping of the extrusion product.
  • the respective fusible conductor block can already comprise an extrusion nozzle connected to it in one piece or be designed as an extrusion nozzle or assume the functions of an extrusion nozzle, so that a separate extrusion nozzle can be dispensed with.
  • the respective outlet of the respective multichannel system on the outlet side of the fusible conductor block is shaped and dimensioned accordingly, so that atomization of the designated polymer melt is realized.
  • the sum of all outlets on the fusible conductor block is referred to as the extrusion nozzle outlet, and the extrusion nozzle outlet can be designed in any height and width depending on the arrangement of the outlets with respect to one another.
  • the extrusion nozzle outlet preferably has a width that is many times greater than its height.
  • the separate extrusion nozzle and, accordingly, also the extrusion nozzle outlet can be manufactured at least partially with an additive manufacturing process.
  • an additive manufacturing process enables the most varied geometries of the extrusion nozzle and the extrusion nozzle outlet as well as corresponding connection means for form-fitting and / or force-fitting connection of the extrusion nozzle to the melt conductor to be produced in a particularly uncomplicated manner.
  • the extrusion nozzle outlet of the extrusion tool is preferably designed with a width of more than 5,000 mm, preferably of more than 6,000 mm or more than 8,000 mm.
  • the extrusion nozzle outlet can be made oversized.
  • faster production and subsequent delivery are more worn or defective parts possible.
  • the extrusion nozzle and / or the extrusion nozzle outlet can be configured in several parts, in particular precisely fitting components with small tolerances can be provided.
  • an extrusion system for producing extrusion products comprising an extrusion tool according to the type described above.
  • the extrusion system is intended in particular for processing polymer melts and for producing extrusion products.
  • the extrusion plant is fed with polymer melt from a supply unit which comprises a silo and / or an extruder or the like.
  • a supply unit which comprises a silo and / or an extruder or the like.
  • Such an extrusion tool has the advantage that, due to its method of manufacture, for example, for maintenance and / or maintenance work, a particularly quick and easy change of the fusible conductor, the fusible conductor block, a possible extrusion nozzle and / or a possible extrusion nozzle outlet at the extrusion nozzle is possible.
  • extrusion products can be produced in oversize, in particular oversized, since the extrusion tool can be designed in any shape and size, in particular in any width.
  • a multi-part design of the fusible conductor with several fusible conductor blocks connected in parallel or in series is possible in order to produce extrusion products with dimensions that were previously not possible, in particular in excess width.
  • the extrusion system according to the invention with the melt conductor according to the invention can be designed as a device for producing filaments or threads.
  • Such devices have in common that they have a point-shaped polymer melt outlet on the extrusion tool or on the fusible conductor block of the fusible conductor, a plurality of small nozzle bores being formed in each case on the outlet side.
  • the threads form what are known as nonwovens, mono- or multifilaments or ribbons, for example.
  • the melt conductor according to the invention is advantageously used as a melt distributor of the shaping extrusion tool for distributing the polymer melt.
  • the melt conductor according to the invention can be used in a device for the production of nonwovens from continuous filaments (a so-called spunbond system), essentially consisting of at least one spinning device for spinning the filaments. te, a cooling device for cooling the filaments, a stretching device for stretching the filaments, a depositing device, in particular a depositing screen belt, for depositing the filaments to form a nonwoven web, a consolidation device for consolidating the filaments of the nonwoven web and a winding device for winding up the nonwoven web.
  • a device for the production of nonwovens from continuous filaments essentially consisting of at least one spinning device for spinning the filaments.
  • a cooling device for cooling the filaments
  • a stretching device for stretching the filaments
  • a depositing device in particular a depositing screen belt
  • a consolidation device for consolidating the filaments of the nonwoven web
  • a winding device for winding up the nonwoven web.
  • the spinning device consists essentially of at least one gravimetric or volumetric metering device for metering and supplying at least one polymer component to an extruder or to a supply unit, at least one extruder or a supply unit for compressing, melting and conveying the at least one polymer component, at least one Melt filter, which is ideally used as a screen changer with or without automatic cleaning to filter particles from the polymer melt, at least one melt and / or spinning pump for conveying the polymer melt, at least one melt conductor designed as a melt distributor, which the polymer melt essentially transversely to the global machine direction or Evenly distributed in so-called “Cross Direction” (CD) of the device, if necessary at least one further melt conductor designed as a melt distributor, which also transfers the polymer melt transversely to the gl Obal machine direction, but also perpendicular to the “Cross Direction” (CD) distributed in a so-called “Machine Direction” (MD) of the device, a single or multi-row nozzle
  • the invention can also be used in a device for producing nonwovens from ultrafine continuous filaments (a so-called meltblown system), essentially consisting of at least one blowing device for producing and subsequent cooling of ultrafine filaments, a depositing device, in particular a depositing roller, for depositing the ultrafine filaments to form a nonwoven web , a consolidation device for consolidating the filaments of the nonwoven web and a winding device for winding up the nonwoven web.
  • a device for producing nonwovens from ultrafine continuous filaments essentially consisting of at least one blowing device for producing and subsequent cooling of ultrafine filaments, a depositing device, in particular a depositing roller, for depositing the ultrafine filaments to form a nonwoven web , a consolidation device for consolidating the filaments of the nonwoven web and a winding device for winding up the nonwoven web.
  • the spinning device essentially consists of at least one gravimetric or volumetric metering device for metering and supplying at least one polymer component to an extruder or a supply unit, at least one extruder or a supply unit for compressing and melting the at least one polymer component, at least one melt filter, ideally as a screen changer with or without automatic cleaning to filter particles from the polymer melt, at least one melt and / or spinning pump to build up continuous pressure of the polymer melt, at least one melt conductor designed as a melt distributor for the polymer melt in "cross direction" (CD) the device evenly distributed, optionally at least one further melt conductor designed as a melt distributor which additionally distributes the polymer melt in “Machine Direction” (MD) of the device, one or more row nozzle tool of the extrusion tool for the production of ultra-fine filaments from polymer melt and pipes and / or hose lines for connecting the above devices.
  • the melt conductor according to the invention is therefore used in particular as a melt distributor for distributing the polymer melt.
  • the extrusion installation according to the invention with the fusible conductor according to the invention can in a further variant be a device for the production of plates or flat films.
  • Such devices have in common that a linear polymer melt outlet is formed on the extrusion tool, in particular on the melt conductor block of the melt conductor, as a result of which the extrusion product has at least one top and bottom.
  • the melt conductor according to the invention is advantageously used as a melt distributor of the shaping extrusion tool for distributing the polymer melt.
  • melt conductors according to the invention can be used in a device for producing flat films (a so-called flat film plant), comprising a device for providing a polymer melt, a slot die or a tool for generating a tabular polymer melt stream and a cooling roller unit.
  • the device for providing a polymer melt consists of at least one gravimetric or volumetric metering device for metering and feeding at least one polymer component for the extruder, at least one extruder for compressing, melting and conveying the at least one polymer component, at least one melt filter, which ideally acts as a screen changer with or without automatic cleaning to filter particles from the polymer melt, optionally from a melt and / or Spinning pump for conveying the polymer melt, optionally from a melt mixer to create a multi-layer structure of the melt flow, a melt conductor designed as a melt distributor for distributing the melt flow in "cross direction" (CD), an extrusion nozzle designed as a slot nozzle for forming a tabular polymer melt flow and pipe - And / or hose lines for connec tion of the above facilities.
  • the melt conductor as a melt distributor, as a melt mixer and in a combination of melt distributor and melt mixer.
  • the extrusion system according to the invention with the fusible conductor according to the invention can be designed in a further variant as a device for producing pipes, profiles or hoses.
  • Such devices provide a polymer melt outlet which generates internal and external surfaces of the extrusion product by means of appropriately designed melt channel guides and / or supplementary fixtures.
  • the melt conductor according to the invention is advantageously used as a melt distributor of the shaping extrusion tool for distributing the polymer melt.
  • the extrusion system according to the invention with the fusible conductor according to the invention can be designed in a further variant as a device for producing a tubular film.
  • a device for producing a tubular film has an at least partially circular line-shaped polymer melt outlet on the extrusion tool, which comprises an annular gap, whereby the extrusion is given an inside and outside.
  • the melt conductor according to the invention is advantageously used as a melt distributor of the shaping extrusion tool for distributing the polymer melt.
  • the melt conductor according to the invention can be used in a device for the production of blown films (a so-called blown film system), essentially consisting of a device for providing a polymer melt or a supply unit, a blow head for producing a film tube, a take-off device for Pulling off and transverse and longitudinal stretching of the film tube in the extrusion direction and a cooling device for cooling the film tube are used.
  • a device for the production of blown films essentially consisting of a device for providing a polymer melt or a supply unit, a blow head for producing a film tube, a take-off device for Pulling off and transverse and longitudinal stretching of the film tube in the extrusion direction and a cooling device for cooling the film tube are used.
  • the device for providing a polymer melt or the provision unit consists of at least one gravimetric or volumetric metering device for metering and feeding at least one polymer component to the extruder, at least one extruder for compressing, melting and conveying the at least one polymer component, at least one melt filter that ideally as a screen changer with or without automatic cleaning to filter particles from the polymer melt, optionally from a melt and / or spinning pump to convey the polymer melt, and pipes and / or hose lines to connect the above devices and the blow head, at least the blow head is to be understood as an extrusion tool according to the invention with a melt distributor integrated in the blow head, in particular a spiral distributor or plate distributor, the blow head comprising an annular slot nozzle with a spiral distributor, in particular a radial spiral distributor iler for forming a single or multi-layer ring-shaped polymer melt stream and an inflation device for inflating a film tube.
  • the melt conductor according to the invention is thus used in particular as a melt distributor
  • the object is achieved by a method for operating an extrusion system according to the embodiment described above, the extrusion system being supplied with at least one extrudable polymer, in particular at least one plastic, which is plasticized to form a respective polymer melt, the respective polymer melt is fed to a melt conductor according to the type described above, which distributes and / or mixes the respective polymer melt.
  • the extrudable polymer is supplied, for example, via a silo or a conveying device that is either part of the extrusion system or a separate component or assembly.
  • the extrudable polymer can be fed to the extrusion plant as granules, that is to say in essentially solid form, or as an at least partially melted melt.
  • granules can be further processed by a supply unit, in particular an extruder or the like, and by melting zen and / or further processing steps are plasticized in such a way that it can be fed to the melt conductor as a polymer melt for combining and / or dividing.
  • a supply unit in particular an extruder or the like
  • melting zen and / or further processing steps are plasticized in such a way that it can be fed to the melt conductor as a polymer melt for combining and / or dividing.
  • the polymer melt After the polymer melt has been divided up and / or brought together, it can be fed from the melt conductor to an extrusion nozzle which processes the polymer melt further to produce the extrusion product.
  • All components of the extrusion system described in the context of this invention as additively manufactured components, in particular the extrusion tool, the fusible conductor and the fusible conductor block, are made of a material suitable for additive manufacturing and / or casting.
  • Metal, plastic and / or ceramic are particularly suitable as the material.
  • the term “plastic” is preferably to be understood as meaning high-performance plastics that allow the extrusion tool to operate at temperatures of over 200 ° C.
  • One advantage of components made additively from ceramic, in particular melt channels made from ceramic additively, is the minimization of deposits.
  • the surfaces of the melt channels that come into direct contact with the polymer melt are designed as a single or multi-layer ceramic layer in the form of an inliner, in a material that differs from the existing melt conductor block.
  • the channels of the respective multi-channel system can have, at least in sections, a single-layer or multi-layer ceramic layer for channel surface modification.
  • the fusible conductor block with the multichannel system can consist of different materials in segments, the advantages of which can be used for the respective application. In particular, these can be different metals, or a combination of metal, ceramic and / or plastic.
  • a surface treatment to refine the surface of the channels of the Multi-channel system can include a heat treatment, a chemical vapor deposition, a physical vapor deposition, an infiltration or the like.
  • a coating is formed in one or more layers, in particular on the channel surfaces of the multi-channel system, whereby the surface texture of the channels of the multi-channel system is influenced, so that advantageously the flow properties of the polymer melt are improved and deposits within the multi-channel system are reduced.
  • the inner surface of the channels of the multi-channel system and, if provided, the coating of the channels can be reworked or treated. On the one hand, this can include cleaning and / or flushing of the multi-channel system. It is also conceivable to carry out flow grinding of the channels of the multichannel system. These steps can also be carried out at maintenance intervals or when changing products in order to loosen and remove any deposits in the multi-channel system.
  • FIG. 1 shows a schematic view of a possible structure of an extrusion system with a fusible link, comprising a fusible link block with a multi-channel system according to a first alternative;
  • FIG. 2 shows a schematic perspective view of the multichannel system according to FIG. 1, the melt conductor being designed as a melt distributor;
  • FIG. 1 shows a schematic view of a possible structure of an extrusion system with a fusible link, comprising a fusible link block with a multi-channel system according to a first alternative;
  • FIG. 2 shows a schematic perspective view of the multichannel system according to FIG. 1, the melt conductor being designed as a melt distributor;
  • FIG. 1 shows a schematic view of a possible structure of an extrusion system with a fusible link, comprising a fusible link block with a multi-channel system according to a first alternative;
  • FIG. 2 shows a schematic perspective view of the multichannel system according to FIG. 1, the melt conductor being designed as a melt distributor;
  • FIG. 3 shows a schematic perspective view of the multichannel system according to a second alternative exemplary embodiment, the melt conductor being designed as a melt mixer;
  • melt conductor being partially designed as a melt distributor and partially as a melt mixer
  • FIG. 5 shows a schematic perspective view of the multichannel system according to a fourth alternative exemplary embodiment, the melt conductor being partially designed as a melt mixer and partially as a melt distributor;
  • 6A shows a schematic perspective view of a fifth alternative exemplary embodiment of the multichannel system, the melt conductor being designed as a melt distributor; 6B shows a further schematic perspective view of the fifth alternative Ausrete approximately example according to FIG. 6A;
  • FIGS. 6A and 6B shows a further schematic perspective view of the fifth alternative exemplary embodiment according to FIGS. 6A and 6B;
  • 7A is a schematic plan view of a sixth alternative(sbei game of the multi-channel system, the melt conductor being designed as a melt distributor;
  • FIG. 7B is a schematic perspective view of the sixth alternative embodiment according to FIG. 7A;
  • FIGS. 7A and 7B Exemplary embodiment according to FIGS. 7A and 7B;
  • FIGS. 7A to 7C shows a schematic perspective view of a seventh alternative exemplary embodiment of the multichannel system, the melt conductor being designed as a melt distributor;
  • FIG. 9 shows a schematic perspective view of an eighth alternative exemplary embodiment of the multichannel system, the fusible conductor being designed as a melt distributor;
  • FIG. 10A shows a schematic perspective view of a ninth alternative exemplary embodiment of the multichannel system, the melt conductor being designed as a melt distributor;
  • FIG. 10B shows a schematic top view of the ninth alternative exemplary embodiment according to FIG. 10A;
  • FIG. 11 shows a schematic partial sectional illustration of a melt channel of a multi-channel system according to a tenth alternative embodiment
  • FIG. 12A shows a schematic partial sectional illustration of a melt channel of a multichannel system according to an eleventh alternative embodiment, a bimetal being shown in an undeformed state;
  • FIG. 12B shows a schematic partial sectional illustration of the melt channel according to FIG. 12A, the bimetal being shown in a deformed state
  • FIG. 13 shows a schematic partial sectional illustration of a melt channel of a multi-channel system according to a twelfth alternative embodiment
  • FIG. 14 shows a schematic partial sectional illustration of a melt channel of a multi-channel system according to a thirteenth alternative embodiment
  • FIG. 16 shows a schematic partial sectional illustration of the fusible conductor block according to a fifteenth alternative embodiment.
  • an extrusion system 3 is shown in a greatly simplified manner.
  • the extrusion system 3 comprises a supply unit 23 which is designed to supply and process a polymer melt 24, in the present case a plastic.
  • the supply unit 23 is designed as an extruder - not shown here - which plasticizes at least one extrudable polymer 29 to form the polymer melt 24.
  • the provision unit 23 can also be designed to provide one or more different polymer melts 24 with the same or different properties.
  • the polymer melt 24 is continuously conveyed from the supply unit 23 into an extrusion tool 2, comprising a melt conductor 1 and an extrusion nozzle 14 downstream of the polymer melt 24 in the designated flow direction 25.
  • the extrusion tool 2 is integrated in the continuously operating extrusion system 3 at which the polymer melt 24 is continuously conveyed through the melt conductor 1 in a global machine direction 18, the terms “downstream” and “upstream” referring to this global machine direction 18.
  • the fusible conductor 1 which is designed as a melt distributor according to this first exemplary embodiment, has a fusible conductor block 4 with a multichannel system 5 extending three-dimensionally within the fusible conductor block 4.
  • the fusible link block 4 is manufactured using an additive manufacturing process and can be integrated into the continuously operating extrusion system 3 as an exchangeable component of the fusible link 1.
  • the multi-channel system 5 according to the first embodiment according to FIG. 1 is shown in greater detail in FIG.
  • the fusible conductor block 4 can be designed as a solid block or filigree with support structures. To this extent, the multichannel system 5 is supported by support structures that are spatially arranged around the multichannel system 5 - not shown here.
  • the supply unit 23 is flanged to an inlet side 26 of the fusible conductor block 4, the extrusion nozzle 14 being formed on the outlet side 27 of the fusible conductor block 4, specifically in such a way that the extrusion nozzle 14 is also manufactured using an additive manufacturing process, namely together with the fusible conductor block 4.
  • a collecting space (not shown here) into which the multi-channel system 5 opens, can be formed on the exit side 27 of the fusible conductor block 4, the collecting space being designed for this purpose that with the as a melt distributor trained melt conductor 1 to receive distributed polymer melt 24 and to feed the Extrusi onsdüse 14 continuously.
  • the collecting space can also be designed in such a way that a perforated disk and / or a filter screen is integrated into it.
  • the multichannel system 5 has one or more outlets 7 which are designed to guide the polymer melt 24 into the collecting space or directly into the extrusion nozzle 14 for feeding the extrusion nozzle 14.
  • the extrusion nozzle 14 shown in Fig. 1 has an extrusion nozzle outlet 22 with a width B of more than 5,000 mm.
  • the width B defines the width of an extrusion product 30 hergestell th by the extrusion system, which is designed as a film according to FIG. 1.
  • the melt conductor 1 distributes the polymer melt 24 according to FIG. 2 in the multichannel system 5 based on its designated flow direction 25 from an inlet 6 arranged on an inlet side 26 of the melt conductor block 4, which in this case is designed as a melt distributor block 4, via several branches 8 arranged one behind the other, several generations 9a, 9b branches 10 as well as several generations of divided melt channels 11 arranged in between to form a multitude of fluidically connected to the inlet 6 and arranged on an outlet side 27 of the fusible conductor block 4.
  • the multi-channel system 5 thus has an inlet 6 and a large number of fluidically connected to the inlet 6 connected outlets 7.
  • the inlet 6 on the inlet side 26 of the melt conductor block 4 is consequently designed as an inlet opening through which the polymer melt 24 is fed into the multi-channel system 5 of the melt conductor block 4.
  • the multi-channel system 5 is shown in FIG. 2 with only one branch 8 and two generations 9a, 9b of further branches 10.
  • the further branches 10 and melt channels are designed essentially analogously to this in order to distribute the polymer melt 24 over the corresponding width B for the extrusion nozzle outlet 22.
  • three or more generations of further branches 10 are also conceivable.
  • a melt channel 11a a-th generation 12a is arranged between the inlet 6 and the branch 8, between the branch 8 and the first generation 9a further branches 10 a b th generation 12b melt channels 11b, and between the first Generation 9a branching branches 10 and the second generation 9b branching branches 10 a c-th generation 12c melt channels 1 lc arranged.
  • the second generation 9b branches 10 is also a d-th generation 12d melt channels l ld downstream.
  • melt channels 11 increases with increasing generation, namely one melt channel 11a of the a-th generation becomes two melt channels 1 lb of the b-th generation, and the two melt channels 1 lb of the b-th generation
  • two melt channels 11c of the c-th generation that is to say a total of four melt channels 11c, will be formed, and so on.
  • the number of melt channels 11 doubles from generation to generation downstream in the direction of flow 25.
  • the multichannel system 5 and its individual cavities, in the present case designed as melt channels 11, branch 8 and further branches 10, are manufactured by means of the additive manufacturing process.
  • cavities can be provided, for example as a collecting space, local widenings 28 or junctions, which will be discussed in more detail in the further description of alternative exemplary embodiments.
  • the cavities can be designed as distributing or mixing chambers (not shown here) or the like.
  • the melt channel 11a of the a-th generation 12a has a first local cross section which is made smaller than the second local cross section of the divided melt channels 11b b-th generation 12b.
  • Each local cross section of the divided melt channels 11b b-th generation 12b is in turn larger than the local cross section of the melt channels 11c c-th generation 12c divided therefrom, and so on.
  • the respective melt channel 11 over at least half the length of the respective melt channel 11, preferably over at least 2/3 the length of the respective melt channel 11, preferably over at least 3/4 of the length of the respective melt channel 11 has a larger or smaller local cross section.
  • the melt channel 11a of the a-th generation 12a is to be oriented in the designated flow direction 25 of the polymer melt 24 to the inlet 6 and the melt channels 11b of the b-th generation 12b with respect to the melt channel 11a of the a-th generation 12a to the outlet 7.
  • the melt channels 11c c-th generation 12c are oriented towards the melt channels l ld d-th generation 12d at the inlet 6, the melt channels l ld d-th generation 12d based on the melt channels 11 a-ter, b-ter and c -th generation 12a, 12b, 12c the respective outlet 7 are to be oriented. It follows from this that the melt conductor 1 functions as a melt distributor.
  • a second alternative multichannel system 5 of a second alternative fusible conductor block 4 - not shown here - the fusible conductor 1, in contrast to FIG is trained.
  • the fuse link 1 has a plurality, in the present case eight inlets 6 on the inlet side 26 of the fuse block 4, via which one or up to eight identical or at least partially different polymer melts 24 are fluidically connected to the inlets 6 and at the Exit side 27 of the fusible conductor block 4 angeord designated outlet 7 are brought together.
  • the fusible conductor block 4 is not shown, but only the multichannel system 5 for better illustration.
  • the multichannel system 5 is designed essentially identically to the exemplary embodiment according to FIG. 2.
  • the multi-channel system 5 in the present case also has several branches 8 arranged one behind the other, several generations 9a, 9b further branches 10 and several generations 12a-12d of divided melt channels 11a-ld arranged between them, but this is to be considered against the designated flow direction 25 of the polymer melt 24, and from the exit side 27 to the entry side 26.
  • a melt channel 11a of the a-th generation 12a are arranged between the respective outlet 7 and the branch 8, and between the branch 8 and the first generation 9a further branches 10 a bth generation 12b melt channels 11b and 11b between the first generation 9a branches 10 and the second generation 9b branches 10 a c-th generation 12c melt channels 11c arranged.
  • the second generation 9b branches 10 is also followed by a d-th generation 12d melt channels l ld, which are fluidically connected directly to the inlets 6.
  • the number of melt channels 11 from the inlets 6 to the outlet 7 decreases with a decreasing generation, namely two of the present eight melt channels l ld d th generation 12d each become one melt.
  • zekanal 11c c-th generation 12c so a total of four melt channels 11c c-th generation 12c.
  • one melt channel 1 lb b-th generation 12b i.e. a total of two melt channels 1 lb b-th generation 12b, emerge, and from the two melt channels 11b b-ter Generation 12b, a melt channel 11a of the a-th generation is formed, which is fluidically connected directly to the outlet 7.
  • the local cross section of the respective melt channel generation in the designated flow direction 25 of the polymer melt 24 increases with each decreasing generation.
  • the melt channels 11a of the a-th generation 12a are oriented in the designated flow direction 25 of the polymer melt 24 to the outlet 7 and the melt channels 11b of the b-th generation 12b are oriented towards the melt channels 11a of the a-th generation 12a to the inlets 6.
  • the melt channels 11c c-th generation 12c are oriented towards the melt channels l ld d-th generation 12d of the outlet 7, the melt channels l ld d-th generation 12d based on the melt channels 11a, 11b, 11c a- ter, b-
  • the 3rd and 3rd generation 12a, 12b, 12c are oriented towards the entrances 6. It follows from this that the fusible conductor 1 functions as a melt mixer.
  • Fig. 4 shows a third alternative multichannel system of a - not shown here - third alternative fusible conductor block 4.
  • the present multichannel system 5 is formed as a combination of a partially formed as a melt distributor and partially as a melt mixer out melt conductor 1.
  • an inlet 6 of the multi-channel system 5 is initially provided, the melt channel i la a-th generation 12a being divided into a plurality of melt channels l ld d-th generation 12d analogously to the exemplary embodiment according to FIG. 2A.
  • melt channels 11 are brought together again analogously to the exemplary embodiment according to FIG. 3 via melt channels 11c, 11b, c'th generation 12c 'and b' -th generation 12b 'to a melt channel 1 la a'-th generation 12a' or the exit occurs 7.
  • a fourth alternative multichannel system 5 of a fourth alternative fusible conductor block 4 (not shown) is shown, in the present case also a combination of a partly as a melt mixer and partly as a melt distributor trained fusible conductor 1 is shown.
  • the mode of operation is carried out in the opposite way.
  • the fusible conductor block 4 has several inlets 6 to the multi-channel system 5 on its inlet side 26, the melt channels l ld d th generation 12d fluidly connected directly to the inlets 6 along the designated flow direction 25 of the polymer melt 24 analogous to the exemplary embodiment according to FIG 3 are brought together from generation to generation to form a melt channel 11a of a-th generation 12a.
  • melt channel 11a of the a-th generation 12a is analogous to the exemplary embodiment according to FIG. 2 via a branch 8, several generations 9a ', 9b', further branches 10 and generations 12b ', 12c', 12d ', melt channels 11b, 11c , l ld divided from generation to generation until a plurality of outlets 7 are arranged on the exit side 27 of the fusible conductor block 4.
  • the multichannel system 5 according to the exemplary embodiment according to FIG. 4 and according to the exemplary embodiment according to FIG. 5 is not limited to the shape and arrangement shown here. It is also conceivable, upstream and / or downstream of the respective multichannel system 5, to provide further sections designed as melt distributors and / or melt mixers, which sections can be designed and combined as desired. However, it is advantageous if the polymer melt 24 always has the same melt history at the outlet 7 or at the outlets 7, regardless of which melt channels 11 or melt channel sequence it flows through. With eight melt channels l ld of the d-th generation 12d, the polymer melt 24 is consequently divided into a maximum of eight different melt streams.
  • the same history of the polymer melt 24 means that all melt streams of the polymer melt 24 at the exit 7 or at the exits 7 have covered the same distance through the multi-channel system 5 and have flowed through the same number of melt channels 11, branches 8 and further branches 10 .
  • the exemplary embodiments according to FIGS. 6A to 10B described below relate exclusively to melt conductors 1 designed as melt distributors, the polymer melt 24 in the multi-channel system 5 being distributed from a respective inlet 6 to a plurality of outlets 7.
  • the arrangement and counting of the generation of the melt channels 11, as well as the branches 8 and generations of the further branches 10 is analogous to the first embodiment according to FIG
  • the following embodiments are also suitable for executing the melt conductor 1 as a melt mixer or as any combination of melt mixer and melt distributor.
  • the multi-channel system 5 is designed to lie essentially in one plane, with the respective inlet 6 and the respective outlet 7 as well as all melt channels 11, branches 8 and further branches 10 in a common plane lie. At least three degrees of freedom are therefore used to form the multi-channel system 5.
  • FIGS. 6A to 6C show a fifth alternative multichannel system 5 of a fifth alternative fusible conductor block 4, the multichannel system 5 in the present case being fanned out three-dimensionally in space using five degrees of freedom.
  • the melt channels 11 run in the flow direction of the polymer melt 24 starting from the inlet 6 and distributed over several generations 12a-12e at least partially down, to the left, to the right, into the plane of the sheet and out of the plane of the sheet out.
  • the melt channels 11a - I le fluidically connected to the inlet 6 are thus distributed over the branches 8 and further branches 10 to the outlets 7, which according to the present division are divided into two essentially parallel planes.
  • the first generation 9a branches 10 is designed such that the melt channels 11c of the c-th generation 12b to the melt channels 1 lb of the b-th generation 12b are rotated by essentially 90 °, so that starting from each of the melt channels 1 lc c-
  • the third generation forms a separate distribution system 29a, 29b, 29c, 29d in such a way that the first and second distribution systems 29a, 29b are arranged in a first level and the third and fourth distribution systems 29c, 29d are arranged in a second level .
  • melt conductor 1 designed in this way, it is possible in a simple manner to distribute the polymer melt 24 not only uniformly across the width analogous to FIG. 2 but also equally across it, i.e. depending on the direction of view in height or depth, around the polymer melt 24 to be able to emerge from the fusible terblock 4 in a comparatively large area.
  • This is particularly suitable for the production of filaments or continuous filaments, in particular for the production of spunbonded nonwovens by means of multi-row nozzle tools.
  • the local cross section of the melt channels 11 decreases from generation to generation 12a-12e up to the outlets 7, with the melt channels 11 of each generation 12a-12e in all distribution systems 29a-29d are always symmetrical and the divided melt flows of the designated polymer melt 24 have the same melt history.
  • the outlets 7 of the first and second distribution system 29a, 29b or the first level lie on an imaginary first straight line and the outlets 7 of the third and fourth distribution system 29c, 29d or the second level lie on an imaginary second straight line. Both lines or both planes are arranged parallel to one another here. Since all melt channels 11 are connected to a single inlet 6, all melt flows at the respective outlet 7 have identical material properties due to the same polymer melt 24.
  • the fusible conductor block 4 also has several inspection openings 13a - 13d to the multi-channel system 5.
  • the inspection openings 13a-13d are arranged in a curve section 46 between an essentially horizontal channel section 47 and an essentially vertical channel section 48 of the melt channel 11c c-th generation 12c, and each extend obliquely upward in the direction of a side surface 49 of the fusible conductor block 4.
  • the inspection openings 13a-13d can be used for checking or flushing the multichannel system 5 and can accordingly in principle be arranged on the multichannel system 5 as desired.
  • the first and second inspection openings 13a, 13b are designed in such a way that they emerge via a respective curve section 50 perpendicular to an essentially vertical side surface 49 of the fusible conductor block 4.
  • the third and fourth inspection openings 13c, 13d are designed, for example, in such a way that they emerge via a respective curve section 50 perpendicular to a horizontal side surface 49 of the fusible conductor block 4.
  • the fusible conductor block 4 has a media channel 20 which extends spatially between the melt channels 11 of the multi-channel system 5, in the present case between the two levels of the distribution systems 29a-29d, and realizes a fluid guide.
  • the fluid flow is used here to control the temperature of the melt conductor block 4 and consequently the polymer melt 24 in the multi-channel system 5.
  • the media channel 20 is not fluidically connected to the melt channels 11 of the multi-channel system 5 and has the effect that the melt conductor 1 and in particular the melt conductor block 4 during the operation of the extrusion system 3 can be tempered.
  • Further media channels of any configuration can also be provided, which are fluidically separated from the melt channels 11 of the multi-channel system 5 in the melt distribution block 4.
  • the other media channels can also be designed in the form of drying shafts, which are provided, for example, to accommodate an electrical line and / or to accommodate a measuring device.
  • FIGS. 7A to 7D a sixth alternative multichannel system 5 of a sixth alternative fusible conductor block 4 (not shown here) is shown, the multichannel system 5 in the present case using six degrees of freedom spreading out three-dimensionally in space.
  • the two melt channels 11b of the bth generation 12b partially run counter to a global machine direction 18.
  • the global machine direction 18 leads from the inlet 6 to the outlet 7 of a designated melt flow of the polymer melt 24.
  • Each melt channel 1 lb of the bth generation 12b has a local machine direction 19 which, depending on the formation and extent of the respective melt channel 11, is in the longitudinal direction of the melt channel 11 can always be aligned in the same way or which can have a changing alignment in the longitudinal direction of the melt channel 11. It can be advantageous here if the local machine direction 19 runs at least partially counter to the global machine direction 18. This is shown in particular in FIG. 7A.
  • the “global machine direction” 18 is to be understood as the arrangement of the fusible conductor 1, in particular the fusible conductor block 4, in the extrusion system 3, the global machine direction 18 running along the designated flow direction between the supply unit and the extrusion nozzle 14 on the fusible conductor block 4.
  • the global machine direction 18 is therefore a spatial extension of the fusible conductor 1, in particular the fusible conductor block 4, in the extrusion system 3, taking into account the inlet side 26 and outlet side 27 of the multi-channel system 5 for the designated polymer melt 24.
  • a “local machine direction” 19 can deviate locally from the global machine direction 18, the local machine direction 19 describing the local orientation of the multi-channel system 5, in particular of the respective melt channel 11 relative to the global machine direction 18.
  • the local machine direction 19 runs coaxially to the longitudinal axis of the Melt channel 11 in the direction of the designated flow direction 25 of the polymer melt 24.
  • the local machine direction 19 can preferably be congruent in sections with the global machine direction 18 if the multi-channel system 5 has an inlet 6 on an inlet side of the fuse block 4 and a fluidically connected to it and coaxially arranged therewith th outlet 7 on one of the inlet side opposite outlet side of the fusible terblocks 4 has.
  • the spatial alignment of the melt channel 11 and thus the local machine direction 19 can in this case be at least partially coaxial with the global machine direction 18.
  • the local machine direction 19 regularly deviates from the global machine direction 18. Since all six degrees of freedom can be used to form the multi-channel system 5, an inclined arrangement of the respective melt channel 4 relative to the global machine direction 18 can be provided on the one hand. However, it is also conceivable and can be advantageous, in particular for saving installation space, for the local machine direction 19 to run in sections in the opposite direction with respect to the global machine direction 18.
  • melt channels 11 of the multichannel system 5 in a special exemplary embodiment can be returned almost to the entry side of the melt conductor 1, in particular the melt conductor block 4.
  • the advantage of guiding the local machine direction 19 of the melt channels 11 opposite to the global machine direction 18 is therefore that the melt conductor 1 or the melt conductor block 4 can be designed in a particularly space-saving manner by guiding the melt channels 11 in any way relative to the global machine direction 18.
  • the Schmelzekanä le 11 can be guided around - not shown here - connection or fastening elements, in particular screws, threads or the like.
  • the inlet 6 and the outlets 7 of the multichannel system 5 are essentially arranged in a first level, the melt channels 11b of the bth generation 12b partially running transversely to this first level, so that the first generation 9a branches 10 on to the first level parallel second plane are arranged.
  • the melt channels 11c c-th generation 12c formed thereon extend partially in the second level and are returned to the first level for further distribution of the polymer melt 24. Due to the three-dimensional guidance of the melt channels 11 in space, and in particular by guiding the local machine direction 19 of the melt channels 11 partly against the global machine direction 18, a broad distribution of the polymer melt 24 is realized in a simultaneously smaller axial installation space, i.e. in the global machine direction 18 of the melt conductor 1 . Consequently, in such a case, the fusible conductor 1 can be made more compact.
  • a fusible conductor block 4 designed in this way makes it possible to distribute the polymer melt 24 in such a way that, in particular, nonwovens with 20 to 10,000 individual filaments per meter of width can be produced.
  • a seventh embodiment with a seventh alternative multichannel system 5 is shown.
  • the multichannel system 5 is essentially identical to the multichannel system 5 according to FIG. 2.
  • the melt distribution block 4 in the present case in the area of the melt channels 11c c-th generation 12c, has a static functional element 21 in the form of a static mixing element as a means for influencing the designated polymer melt 24.
  • the respective static functional element 21 is arranged within a local widening 28 of the melt channels 11c c-th generation 12c and is designed in the form of intersecting struts.
  • the respective functional element 21 is arranged in one of the melt channels 11c c-th generation 12c between a branch 10 of the first generation 9a and a branch 10 of the second generation 9b. Before and after the local widening 28, the respective melt channel 11c c-th generation 12c has essentially the same cross-sectional size and shape.
  • the respective static functional element 21 realizes a thorough mixing of the polymer melt 24 guided and distributed within the melt channels 11c c-th generation 12c. This in turn ensures a more uniformity of the melt strand of the polymer melt 24 guided in the respective melt channel 11, in particular its flow and material properties become.
  • the static mixing element can alternatively also be arranged directly in the respective melt channel 11 and thus not be formed in a local expansion.
  • an eighth exemplary embodiment according to FIG. 9 shows an eighth alternative multichannel system 5 which, instead of the widening 29 with the functional element 21 arranged therein, has a respective pump 36 as a means for at least indirectly influencing the polymer melt 24 on the respective melt channel 11c c-th generation 12c is arranged to convey the polymer melt 24 through the multi-channel system 5.
  • the provision of pumps 36 is advantageous in multi-channel systems with a large number of melt channel generations and branch generations, the polymer melt 24 being distributed over a large width of the fusible conductor block 4 or brought together by a large width of the fusible conductor block 4.
  • the exemplary embodiment according to FIG. 9 can easily be combined with the exemplary embodiment according to FIG. 8.
  • FIGS. 10A and 10B show a ninth alternative exemplary embodiment of a ninth alternative multi-channel system 5.
  • the multi-channel system 5 is designed essentially analogously to the multi-channel system 5 according to FIG. 2.
  • the fusible conductor block 4 also has a through-opening 17, likewise designed as a channel system, which is fluidically connected to the multi-channel system 5 in the area of the outlets 7 of the multi-channel system 5 via junctions 15 in order to transfer a medium to the multi-channel system 5 and / or or lead away from the multi-channel system 5.
  • the through opening 17 for adding an additive to the melt channel l ld d-th generation 12d of the multi-channel system 5 is formed.
  • an additive (not shown here) is fed into a first inlet 38 of the through opening 17, the additive being distributed over the channels 39 in such a way that each channel 39 of the through opening 17 via a respective junction 15 with one Melt channel 1 ld d-th generation 12d of the multi-channel system 5 is connected.
  • the additive is mixed with the polymer melt 24 by means of the merges 15 in order to set material properties of the polymer melt 24, for example.
  • the through opening 17, which is designed as a channel system, also has channels 39, analogous to the multi-channel system 5, which are divided over branches 8 and several generations 9a further branches 10, so that a corresponding supply of the melt flowing in the melt channels l ld d-th generation 12d of the multi-channel system 5 flows of the polymer melt 24 with additives can take place.
  • the polymer melt 24 in the multi-channel system 5 and the additive in the through-opening 17 are only brought together shortly before exiting the multi-channel system or from the fusible conductor block 4. This creates a compound which is atomized via the outlets 7 or is fed to an extrusion nozzle (not shown here).
  • the channels 39 of the through-opening 17 can be arranged parallel, perpendicular or at an angle to the melt channels 11 of the multi-channel system 5.
  • the channels 39 of the through-opening 17 carrying the additive are arranged at an angle in such a way that the channels 39 constantly approach the melt channels 11a-11d of the multichannel system 5 from generation to generation until the channels 39 and the melt channels 11dd -ter generation 12d meet in the area of the respective merging 15 and realize a mixing of the designated polymer melt 24 with the designated additive.
  • venting that is to say a discharge of gases from the multichannel system 5 can also take place via the channel system of the through opening 17.
  • the junctions 15 can also be arranged at other points of the multichannel system 5, in particular in the area of a different generation of melt channels 11 or branches 8 or further branches 10.
  • FIGS. 11 to 16 various embodiments of means for at least indirectly influencing the polymer melt 24 are shown. These can be arranged in individual melt channels 11, in several melt channels 11 of a generation or in all melt channels 11 of the multi-channel system 5 and can be combined with one another as required or depending on the requirements for the polymer melt and / or the extrusion product 30.
  • FIG. 11 shows a partial sectional illustration of a melt channel 11 of the multichannel system 5 - not shown here in greater detail - according to a tenth alternative embodiment.
  • the means for at least indirectly influencing the Polymer melt 24 has an actuator 33 which drives a wheel 40 which is arranged inside the melt channel 11 and is rotatably mounted about an axis of rotation R.
  • the axis of rotation R of the wheel 40 runs transversely to the designated flow direction 25 of the polymer melt 24.
  • the rotation of the wheel 40 is controlled and regulated by means of a control unit 44 arranged outside the fusible conductor block 4, this being an adaptation of a direction of rotation and / or a rotational speed or rotational speed and / or an activation or deactivation of a rotation of the wheel 40.
  • a thorough mixing and homogenization of the polymer melt 24 flowing in the flow direction 25 - not shown here - is realized by the wheel 40.
  • the actuator 33 can be activated or deactivated as a function of the material properties, in particular the flow properties of the polymer melt 24.
  • the actuator 33 comprises a drive unit - not shown here - for driving the wheel 40, which is likewise arranged within the fusible conductor block 4 and in the area of the melt channel 11.
  • the axis of rotation R of the wheel 40 can alternatively also be arranged parallel to the designated flow direction 25 of the polymer melt 24, so that the wheel 40 realizes a thorough mixing of the polymer melt 24 in the form of a propeller, rotor or turbine wheel. Furthermore, it is conceivable to arrange the wheel 40 without being driven in the melt channel 11.
  • the means for at least indirectly influencing the polymer melt 24 is designed as a bimetal 34 according to an eleventh alternative embodiment.
  • the bimetal 34 is arranged circumferentially around the melt channel 11 and consists of a first layer 41a and a second layer 41b arranged radially outside thereof, the second layer 41b being in full contact with the first layer 41a.
  • the bimetal 34 is also produced by means of an additive manufacturing process, to be precise during the formation of the melt channel 11.
  • the layers 41a, 41b of the bimetal are formed from two different metals which have different coefficients of thermal expansion, the metals being materially and / or positively connected to one another. Due to the different coefficients of thermal expansion of the metals, one of the layers 41a, 41b, in this case the first layer 41a, expands as a result of the fusible conductor block 4 heating up and / or the polymer melt 24 more strongly than the other, whereby the bimetal is locally deformed.
  • the melt channel 11 has a first diameter D1, which is larger than a second diameter D2 of the melt channel 11, shown in FIG. 12B, which occurs when the bimetal 34 is heated sets a second temperature.
  • the bimetal 34 or the metallic layers 41a, 41b of the bimetal 34 can be designed in such a way that the local cross-section of the melt channel is widened as a result of heating 11 takes place so that D2 is greater than Dl.
  • FIG. 13 a partial longitudinal section of a melt channel 11 according to a twelfth exemplary embodiment is shown, in the present case a part 35 movably arranged in the melt channel 11 being arranged as a means for influencing the polymer melt 24.
  • the movably arranged part 35 is a wheel 40 rotatably arranged with respect to the fusible conductor block 4 or the wall of the melt channel 11, which rotates around an axis of rotation R due to kinetic energy of the polymer melt 24 flowing in the designated flow direction 25 and mixes the polymer Melt 24 is made possible essentially analogously to FIG. 11.
  • the means for at least indirect influencing of the polymer melt 24 comprise a manipulation device 32 that can be selected and alternately activated and deactivated for manipulating from within the fuse block 4 for guiding Polymer melt 24 established melt areas.
  • the designated polymer melt 24 guided within the melt channels 11 is influenced by switching the manipulation device 32 on or off.
  • the manipulation device 32 is designed to be temperature-controlled. This means that by means of the manipulation device 32, depending on the temperature of the material of the fusible conductor block 4 and / or depending on the temperature of the polymer melt 24, a control, a change in the properties of the polymer melt 24 takes place.
  • the manipulation device 32 is designed as a heating strip, which is arranged at least partially circumferentially and radially spaced from the melt channel 11.
  • the heating strip is shaped like a sleeve, with the heating strip being activated or deactivated as a function of the temperature of the designated polymer melt 24.
  • Activation of the manipulation device 32 may be necessary, for example, in order to reduce the viscosity of the designated polymer melt 24.
  • heating elements and / or heating strips of the manipulation device 32 are effectively arranged as a means for at least indirectly influencing the designated polymer melt 24 on the outer surfaces of the fusible conductor block 4 in order to achieve complete or regional temperature control of the fusible conductor block 4 and thus that within the fusible conductor block 4 to realize polymer melt 24 guided in the melt channels 11.
  • the multi-channel system 5 is partially shown, with an exchangeable plug-in element 31 being received in a recess 42 of the fusible conductor block 4 - shown here in dashed lines - and configured to locally change a channel geometry of at least one of the melt channels 11 and / or at least two of the melt channels 11 of the Multi-channel system 5 to connect fluidically with one another.
  • the plug-in element 31 has a branch 8 which divides a first melt channel 11a into two second melt channels 11b of a generation downstream in the flow direction 25 of the designated polymer melt 24.
  • the plug-in element 31 is designed in such a way that a local cross section of the melt channels 11a, 11b remains constant.
  • the cross-sectional shape and / or the type of cross-section of the melt channels 1 la, 1 lb within the plug-in element 31 changes.
  • means for at least indirect influencing of the polymer melt 24 within the plug-in element 31, as described in FIGS. 11 to 14 or 16 are.
  • the flow properties of the polymer melt 24 can be adapted and / or a melt flow of the multichannel system 5 can be changed.
  • the means for at least indirectly influencing the polymer melt 24, is designed as a cross-section changer 37, specifically in the present case as a valve.
  • the cross section changer 37 - not shown here - is exchangeable in the fusible conductor block 4 - only partially shown here - and is inserted via an external access 45 into a valve seat 16 which is formed in the melt channel 11.
  • the cross-section changer 37 is designed in such a way that the melt channel 11 is sealed off from the external access 45.
  • the cross-section changer 37 designed as a valve is designed to adapt a flow rate of the melt channel 11, wherein the flow rate can be changed during the operation of the extrusion system 3. Due to the exchangeable arrangement of the cross-section modifier 37 on the fusible conductor block 4, the external access 45 can also be provided as an inspection opening or as a passage opening for adding or discharging a medium to or from the multichannel system 5.
  • the means for at least indirect influencing of the polymer melt for example in the form of a flap - not shown here - or any movable wall that can be actuated, for example, with an actuator, individual melt channels and, as a result, individual or several segments of the multi-channel system can be temporarily closed, whereby it is possible to use the extrusion tool to produce extrusion products with different widths or to change the widths continuously.

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Abstract

La présente invention concerne un convoyeur de matière fondue (1), en particulier un distributeur de matière fondue ou un mélangeur de matière fondue, pour un outil d'extrusion (2) d'un système d'extrusion (3), comprenant un bloc de convoyeur de matière fondue (4) ayant un système à canaux multiples (5), le système à canaux multiples (5) étant agencé de telle sorte qu'il s'étend en trois dimensions à l'intérieur du bloc de convoyeur de matière fondue (4) et présente au moins une entrée (6) et au moins une sortie (7) pour un polymère à l'état fondu, de multiples ramifications (8) disposées les unes après les autres et de multiples générations (9a) de ramification supplémentaires (10) étant formées sur de multiples générations (12a, 12b) de canaux de matière fondue distribués (11a, 11b) entre une entrée (6) et une sortie (7) en communication fluidique avec l'entrée (6), m canaux de matière fondue (11a) de l'a-ème génération (12a) ayant des x-èmes sections transversales locales étant prévus et n canaux de matière fondue (11b) de la génération de la b-ème génération (12b) ayant y-èmes sections transversales locales, n > m, si b > a, les y-èmes sections transversales locales des canaux de matière fondue (11b) de la génération de la b-ème génération (12b) sont plus petites que les x-èmes sections transversales locales des canaux de matière fondue (11a) de l'a-ème génération (12a), et des moyens pour influencer au moins indirectement le polymère à l'état fondu étant disposés dans la zone du système à canaux multiples (5).
EP20800002.6A 2019-10-15 2020-10-14 Convoyeur de matière fondue pour outil d'extrusion de système d'extrusion, outil d'extrusion, système d'extrusion et procédé d'actionnement de système d'extrusion de ce type Pending EP4045281A1 (fr)

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DE102019007153 2019-10-15
DE102020118214 2020-07-10
PCT/DE2020/200087 WO2021073697A1 (fr) 2019-10-15 2020-10-14 Convoyeur de matière fondue pour outil d'extrusion de système d'extrusion, outil d'extrusion, système d'extrusion et procédé d'actionnement de système d'extrusion de ce type

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EP20800001.8A Active EP4045280B1 (fr) 2019-10-15 2020-10-14 Convoyeur de matière fondue pour un outil d'extrusion d'un système d'extrusion, outil d'extrusion, système d'extrusion et méthode de fonctionnement d'un tel système d'extrusion
EP20828267.3A Pending EP4045282A1 (fr) 2019-10-15 2020-10-14 Conducteur de fusion pour un outil d'extrusion d'un système d'extrusion, outil d'extrusion, système d'extrusion et procédé de fonctionnement d'un tel système d'extrusion

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EP20828267.3A Pending EP4045282A1 (fr) 2019-10-15 2020-10-14 Conducteur de fusion pour un outil d'extrusion d'un système d'extrusion, outil d'extrusion, système d'extrusion et procédé de fonctionnement d'un tel système d'extrusion

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EP (3) EP4045281A1 (fr)
JP (1) JP2022551894A (fr)
KR (1) KR20220083705A (fr)
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BR (1) BR112022007227A2 (fr)
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US10030321B1 (en) * 2015-04-26 2018-07-24 Thomas M. Tao Extrusion die for making film, fibers, and nanofibers
CN208410607U (zh) * 2018-07-24 2019-01-22 勃乐氏密封系统（太仓）有限公司 恒温式冷流道注射模

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DE112020005051A5 (de) 2022-10-27
WO2021073696A1 (fr) 2021-04-22
JP2022551894A (ja) 2022-12-14
EP4045280B1 (fr) 2024-04-10
US20240100761A1 (en) 2024-03-28
WO2021073697A1 (fr) 2021-04-22
EP4045280A1 (fr) 2022-08-24
CN114555328A (zh) 2022-05-27
EP4045282A1 (fr) 2022-08-24
US20240100762A1 (en) 2024-03-28
DE102020212987A1 (de) 2021-04-15
US20240131769A1 (en) 2024-04-25
BR112022007227A2 (pt) 2022-07-05
DE112020005000A5 (de) 2022-08-25
WO2021073695A1 (fr) 2021-04-22
DE112020005041A5 (de) 2022-10-27
KR20220083705A (ko) 2022-06-20
CN114728458A (zh) 2022-07-08
CN114555328B (zh) 2024-01-05

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