BE1001610A4 - EXTRUDER DIE FOR MANUFACTURING A MULTI-blown film. - Google Patents
EXTRUDER DIE FOR MANUFACTURING A MULTI-blown film. Download PDFInfo
- Publication number
- BE1001610A4 BE1001610A4 BE8700016A BE8700016A BE1001610A4 BE 1001610 A4 BE1001610 A4 BE 1001610A4 BE 8700016 A BE8700016 A BE 8700016A BE 8700016 A BE8700016 A BE 8700016A BE 1001610 A4 BE1001610 A4 BE 1001610A4
- Authority
- BE
- Belgium
- Prior art keywords
- die
- transfer channel
- outlet slot
- annular outlet
- annular
- Prior art date
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Classifications
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- 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
- B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
- B29C48/34—Cross-head annular extrusion nozzles, i.e. for simultaneously receiving moulding material and the preform to be coated
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- 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
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
-
- 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
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
- B29C48/10—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
-
- 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
- B29C48/14—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the particular extruding conditions, e.g. in a modified atmosphere or by using vibration
- B29C48/147—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the particular extruding conditions, e.g. in a modified atmosphere or by using vibration after the die nozzle
- B29C48/1472—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the particular extruding conditions, e.g. in a modified atmosphere or by using vibration after the die nozzle at the die nozzle exit 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
- B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
- B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
- B29C48/21—Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
-
- 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
- B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
-
- 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
- B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
- B29C48/335—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles
- B29C48/336—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles the components merging one by one down streams in the die
- B29C48/3366—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles the components merging one by one down streams in the die using a die with concentric parts, e.g. rings, cylinders
-
- 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
- B29C2791/00—Shaping characteristics in general
- B29C2791/004—Shaping under special conditions
- B29C2791/007—Using fluid under pressure
-
- 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
- B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
- B29C48/335—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
...à partir de plusieurs matières thermoplastiques stratifiées comprenant une partie inférieure de filière (1) équipée d'un dispositif pour l'amenée de plusieurs flux de matière plastique par l'intermédiaire de plusieurs conduits d'amenée (2) une partie supérieure de filière (3) avec fente annulaire de sortie (4) pour la sortie d'un flux de matière plastique multicouche sous forme de gaine, un noyau de filière (5) et un dispositif de stratification (6). Des canaux de transfert (7, 8) en forme de fente annulaire sont disposés dans les parties supérieure (3) et inférieure (1) de la filière.... from several laminated thermoplastic materials comprising a lower part of the die (1) equipped with a device for supplying several flows of plastic material via several supply conduits (2) an upper part of die (3) with annular outlet slot (4) for the exit of a flow of multilayer plastic material in the form of a sheath, a die core (5) and a laminating device (6). Transfer channels (7, 8) in the form of an annular slot are arranged in the upper (3) and lower (1) parts of the die.
Description
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EMI1.1
"Filière d'extrudeuse pour la fabrication d'une feuille soufflée multicouche"
L'invention concerne une filière d'extrudeuse pour la fabrication, par co-extrusion, d'une feuille soufflée multicouche ä partir de plusieurs matières thermoplastiques stratifiées, comprenant une partie inférieure de filière équipée d'un dispositif pour l'amenée de plusieurs flux de matière plastique par l'intermédiaire de plusieurs conduits d'amenée, une partie supérieure de filière avec fente annulaire de sortie pour la sortie d'un flux de matière plastique. multicouche sous forme de gaine, un noyau de filière et un dispositif de stratification, des canaux de transfert en forme de fente annulaire étant disposes dans les parties inférieure et supérieure de la filière.
On entend par dispositif de stratification la somme des mesures mécaniques qui assurent une stratification sans mélange. Cela comprend une prise en considération des flux massiques qui s'additionnent lors de la stratification et l'empechement de l'apparition d'efforts de cisaillement entre les differentes couches par des différences de vitesses ou des mesures analogues. 11 va de soi que dans la filière d'extrudeuse du genre précité, les parties inférieure et superieure de la filière sont disposées ä symétrie de révolution autour de l'axe de la filière, ä l'exception des conduits d'amenée. D'une manière analogue, les canaux de transfert et la fente annulaire de sortie sont conformés, eux aussi, ä symétrie de revolution.
De plus, il va de soi que le noyau peut comporter un système d'arrivée d'air de soufflage et éventuellement aussi un Systeme d'eva- cuation d'air de soufflage lorsqu'il s'agit de la fabrication de feuilles soufflées.
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Dans la filière d'extrudeuse du genre décrit, bien connue dans la pratique, les conduits d'amenée de la partie inférieure de la filière débouchent respectivement dans un canal de transfert particulier. Le dispositif de stratification se trouve dans la partie supérieure de la filière. 11 se compose d'une pluralité de distributeurs ä hélice correspondant à une pluralité de flux de matière plastique, qui sont emboîtés les uns dans les autres et raccordés ä la pluralité des canaux de transfert auxquels fait suite un canal se rétrécissant coniquement en direction de la fente annulaire de sortie dans laquelle se produit la stratification proprement dite.
Les distributeurs ä hélice sont montés en amont parce que les canaux de transfert pour la pluralité des flux de matière plastique sont divises dans la partie supérieure de la filière par des barrettes de noyau qui immobilisent ou supportent le noyau. Des influences gênantes sur les flux de matière plastique doivent être supprimées dans les distributeurs ä hélice avant de pouvoir réaliser la stratification de telle fagon que, sur ce point, les distributeurs ä hélice font partie du dispositif de stratification et le rendent compliqué et coûteux. Le temps de service sans défaillance est souvent insuffisant parce que de la matière plastique peut rester coincée dans les distributeurs ä hélice.
Dans ce cas, 11 est nécessaire de procéder à un démontage coûteux des distributeurs ä hélice emboXtés les uns dans les autres ; à leur nettoyage et à leur remontage.
La présente invention a pour objet de perfectionner une filière d'extrudeuse du genre précité de telle fagon qu'il n'est plus nécessaire de prévoir une partie supérieure de filière avec une pluralité de distributeurs ä hélice emboîtés.
Selon l'invention, ce but est atteint par le fait que les conduits d'amenée débouchent dans un seul canal de transfert en forme de fente annulaire dépourvu de barrettes de noyau et entourant le noyau de la filière, ledit canal de transfert étant conformé en dispositif de stratification, et
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que la fente annulaire de sortie est raccordée au dispositif de stratification par l'intermédiaire d'un seul canal de transfert, sans barrettes de noyau, de la partie supérieure de la filière. L'invention met à profit la découverte qU'11 n'est pas nécessaire pour une filière d'extrudeuse du type décrit ci-dessus de placer le dispositif de stratification dans la partie superieure de la filière, peu avant la fente annulaire de sortie.
En logeant le dispositif de stratification dans la partie inférieure de la filière et en adoptant, par ailleurs, la disposition décrite, il est étonnant de constater qu'aucun mélange ne se produit sur le parcours ultérieur du flux de matière plastique multicouche, entre e dispositif de stratification et la fente annulaire de sortie.
De plus, l'invention met ä profit le fait que des barrettes ne sont plus nécessaires pour le maintien ou la fixation du noyau de la filière lorsque les conduits d'amenee debouchent dans l'unique canal de transfert en forme de fente annulaire qui entoure le noyau de la filière.
Pour la filière d'extrudeuse selon l'invention, il peut être avantageux d'adapter l'épaisseur de la fente annu- laire de sortie aux conditions de service spéciales et aux matières plastiques mises en oeuvre. Pour cela, il est prévu selon l'invention que la fente annulaire de sortie est conformée en tant qu'embouchure d'une section conique du canal de transfert dans la partie supérieure de la filière, qui est disposée entre un element de buse supérieur et un élément de buse inférieur. La largeur de la fente annulaire de sortie peut alors etre variable par réglage ou par remplacement d'au moins l'un des elements de buse. Cette Operation peut également etre effectuée pendant la production et influencée par des mesures relevant de la technique du réglage.
Pour assurer partout des conditions homogènes sur la circonférence de la feuille soufflée, ce qui comprend également une resistance régulière ä 1'écoulement pour le flux de matière plastique stratifiée, 1'invention recommande de placer dans le canal de transfert, dans le sens d'écoulement du flux de matière plastique multicouche et en amont de la section conique du canal de transfert, des ondulations qui s'etendent essentiellement dans le sens circonferentiel.
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Les avantages obtenus résident dans le fait que, tout en renonçant à des distributeurs à hélice emboîtés les uns dans les autres, la filière d'extrudeuses selon l'invention permet sans difficulté la fabrication de feuilles soufflées multicouches réalisées à partir des matières thermoplastiques les plus diverses. De plus, la filière d'extrudeuse selon l'invention peut être réalisée facilement et entretenue sans grandes dépenses.
La description qui va suivre, en regard du dessin annexé à titre d'exemple non limitatif, permettra de bien comprendre comment l'invention peut etre mise en pratique.
La figure unique représente une coupe axiale d'une moitié d'une filière d'extrudeuse selon l'invention comportant les conduits d'amenée.
La filière d'extrudeuse représentée à la figure est destinée à la fabrication, par co-extrusion, d'une feuille soufflée multicouche ä partir de plusieurs matieres thermoplastiques stratifiées. Elle comprend fondamentalement une partie inférieure de filière 1 avec dispositif pour l'amenée de plusieurs flux de matlere plastique, par l'inter- médiaire d'une pluralité de conduits d'amenée 2, une partie supérieure de filière 3 avec fente annulaire de sortie 4 pour la sortie d'un flux de matière plastique multicouche sous forme de gaine, un noyau de filière 5 et un dispositif de stratification 6.
Sont prévus, par ailleurs, des canaux de transfert 7,8 dont l'un 7 est disposé dans la partie inférieure de filière 1, alors que l'autre 8 se situe dans lapartle supê- rieure de filière 3. Le canal de transfert 8 de la partie supérieure de filière 3 débouche dans 1a fente annulaire de sortie 4.
Les conduits d'amenée 2 débouchent dans le canal de transfert 7 unique, en forme de fente annulaire, dans la partie inférieure de filière 1, qui entoure le noyau de filière 5 et qui est dépourvu de barrettes de noyau. 11 ressort nettement du dessin que ce canal de transfert 7 est conformé en dispositif de stratification 6, ä savoir de telle fagon que les flux massiques peuvent s'additionner.
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Sur le plan de la conception, on a alors veillé soigneusement à ce que des efforts de cisaillement entre les differents flux de matière plastique soient évités par des différences de vitesse ou des mesures analogues. La fente annulaire de sortie 4 est raccordée ä ce dispositif de stratification 6 par l'intermediaire d'un seul canal de transfert 8 sans barrettes de noyau dans la partie supérieure de la filière.
Dans l'exemple de réalisation et selon un mode de réalisation préféré de 1'invention, 1a disposition a été choisie de telle façon que la fente annulaire de sortie 4 est conformée en embouchure d'une section conique 9 du canal de transfert 8 dans la partie supérieure de filière 3, laquelle section est disposée entre un element de buse supe- rieur 10 et un é1ément de buse inférieur 11. La largeur de la fente annulaire de sortie 4 peut donc etre modifiée par réglage ou par remplacement d'au moins l'un des é1éments de buse 10,11.
Vues dans le sens de 1'écoulement du flux de matière plastique multicouche, des ondulations 1. qui s'étendent essentiellement dans le sens circonférentiel et sont visibles dans la partie du dessin représentée à plus grande échelle, sont disposées dans le canal de transfert 8, en amont de la section conique 9 du canal de transfert 8.
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EMI1.1
"Extruder die for the production of a multi-layer blown sheet"
The invention relates to an extruder die for the production, by co-extrusion, of a multi-layer blown sheet from several laminated thermoplastic materials, comprising a lower die part equipped with a device for feeding multiple streams. of plastic material via several supply conduits, an upper part of the die with an annular outlet slot for the exit of a flow of plastic material. multilayer in the form of a sheath, a die core and a laminating device, transfer channels in the form of an annular slot being arranged in the lower and upper parts of the die.
The term stratification device is understood to mean the sum of the mechanical measurements which ensure stratification without mixing. This includes taking into account the mass fluxes which add up during the stratification and the prevention of the appearance of shearing forces between the different layers by differences in speeds or similar measurements. It goes without saying that in the extruder die of the aforementioned kind, the lower and upper parts of the die are arranged in symmetry of revolution about the axis of the die, with the exception of the supply conduits. Similarly, the transfer channels and the annular outlet slit are also shaped to be symmetrical in revolution.
In addition, it goes without saying that the core may include a supply air supply system and possibly also a supply air exhaust system when it comes to the production of blown sheets.
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In the extruder die of the type described, well known in the art, the supply conduits of the lower part of the die open respectively into a particular transfer channel. The stratification device is located in the upper part of the die. 11 consists of a plurality of helical distributors corresponding to a plurality of plastic flows, which are nested one inside the other and connected to the plurality of transfer channels which is followed by a channel narrowing conically in the direction of the annular outlet slot in which the actual stratification occurs.
The propeller distributors are mounted upstream because the transfer channels for the plurality of plastic flows are divided in the upper part of the die by core bars which immobilize or support the core. Inconvenient influences on the plastic flows must be removed in the vane distributors before they can be laminated in such a way that, on this point, the vane distributors are part of the laminating device and make it complicated and expensive. Failure-free service time is often insufficient because plastic can become trapped in the vane valves.
In this case, it is necessary to carry out an expensive disassembly of the propeller valves fitted together; cleaning and reassembly.
The object of the present invention is to improve an extruder die of the aforementioned kind in such a way that it is no longer necessary to provide an upper die part with a plurality of nested propeller distributors.
According to the invention, this object is achieved by the fact that the supply conduits open into a single transfer channel in the form of an annular slot devoid of core strips and surrounding the core of the die, said transfer channel being shaped as layering device, and
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that the annular outlet slot is connected to the laminating device by means of a single transfer channel, without core bars, from the upper part of the die. The invention takes advantage of the discovery that it is not necessary for an extruder die of the type described above to place the laminating device in the upper part of the die, shortly before the annular outlet slot.
By accommodating the stratification device in the lower part of the die and by adopting, moreover, the arrangement described, it is astonishing to note that no mixing occurs on the subsequent course of the flow of multilayer plastic material, between th device laminate and the annular outlet slot.
In addition, the invention takes advantage of the fact that bars are no longer necessary for holding or fixing the core of the die when the supply conduits open into the single transfer channel in the form of an annular slot which surrounds the core of the industry.
For the extruder die according to the invention, it may be advantageous to adapt the thickness of the annular outlet slot to the special operating conditions and to the plastics used. For this, it is provided according to the invention that the annular outlet slot is shaped as the mouth of a conical section of the transfer channel in the upper part of the die, which is arranged between an upper nozzle element and a lower nozzle element. The width of the annular outlet slot can then be variable by adjusting or replacing at least one of the nozzle elements. This Operation can also be carried out during production and influenced by measurements relating to the adjustment technique.
To ensure uniform conditions everywhere on the circumference of the blown sheet, which also includes a regular resistance to flow for the flow of laminated plastic material, the invention recommends placing in the transfer channel, in the direction of flow of the multilayer plastic flow and upstream of the conical section of the transfer channel, undulations which extend essentially in the circumferential direction.
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The advantages obtained reside in the fact that, while dispensing with vane distributors nested one inside the other, the extruder die according to the invention allows without difficulty the production of multi-layer blown sheets produced from the most thermoplastic materials. various. In addition, the extruder die according to the invention can be produced easily and maintained without great expense.
The description which follows, with reference to the attached drawing by way of nonlimiting example, will make it possible to understand clearly how the invention can be put into practice.
The single figure shows an axial section of one half of an extruder die according to the invention comprising the supply conduits.
The extruder die shown in the figure is intended for the manufacture, by co-extrusion, of a multi-layer blown sheet from several laminated thermoplastic materials. It basically comprises a lower part of the die 1 with a device for supplying several plastic material flows, via a plurality of supply conduits 2, an upper part of the die 3 with an annular outlet slot. 4 for the outlet of a flow of multilayer plastic material in the form of a sheath, a die core 5 and a stratification device 6.
There are, moreover, transfer channels 7,8 one of which 7 is arranged in the lower part of die 1, while the other 8 is located in the upper part of die 3. The transfer channel 8 of the upper die 3 opens into the annular outlet slot 4.
The supply conduits 2 open into the single transfer channel 7, in the form of an annular slot, in the lower part of die 1, which surrounds the die core 5 and which is devoid of core bars. It is clear from the drawing that this transfer channel 7 is configured as a stratification device 6, that is to say in such a way that the mass fluxes can add up.
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In terms of design, care was then taken to ensure that shear forces between the different plastic flows are avoided by differences in speed or similar measures. The annular outlet slot 4 is connected to this laminating device 6 by means of a single transfer channel 8 without core bars in the upper part of the die.
In the embodiment and according to a preferred embodiment of the invention, the arrangement has been chosen in such a way that the annular outlet slot 4 is shaped into a mouth of a conical section 9 of the transfer channel 8 in the upper part of die 3, which section is arranged between an upper nozzle element 10 and a lower nozzle element 11. The width of the annular outlet slot 4 can therefore be modified by adjusting or replacing at least 1 'one of the nozzle elements 10,11.
Viewed in the direction of flow of the multilayer plastic flow, corrugations 1. which extend essentially in the circumferential direction and are visible in the part of the drawing shown on a larger scale, are arranged in the transfer channel 8 , upstream of the conical section 9 of the transfer channel 8.
Claims (3)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19863601345 DE3601345A1 (en) | 1986-01-18 | 1986-01-18 | EXTRACTION TOOL FOR THE PRODUCTION OF A MULTILAYER TUBULAR FILM |
Publications (1)
Publication Number | Publication Date |
---|---|
BE1001610A4 true BE1001610A4 (en) | 1989-12-19 |
Family
ID=6292096
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BE8700016A BE1001610A4 (en) | 1986-01-18 | 1987-01-16 | EXTRUDER DIE FOR MANUFACTURING A MULTI-blown film. |
Country Status (10)
Country | Link |
---|---|
BE (1) | BE1001610A4 (en) |
DD (1) | DD253216A5 (en) |
DE (1) | DE3601345A1 (en) |
FI (1) | FI870132A (en) |
FR (1) | FR2593112B1 (en) |
GB (1) | GB2185931B (en) |
IT (1) | IT1201161B (en) |
NL (1) | NL8700104A (en) |
NO (1) | NO870158L (en) |
SE (1) | SE8700129L (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3720560C1 (en) * | 1987-06-22 | 1988-09-15 | Bekum Maschf Gmbh | Coextrusion head |
DE9216920U1 (en) * | 1992-10-13 | 1994-02-24 | Windmöller & Hölscher, 49525 Lengerich | Extrusion tool for the extrusion of melt hoses |
US7264836B2 (en) | 2003-03-21 | 2007-09-04 | Kraft Foods Holdings, Inc. | Production of triple coextruded baked bar goods |
DE102004001473B4 (en) * | 2003-11-10 | 2006-05-11 | Kuhne Gmbh | Film die |
US7470119B2 (en) | 2004-05-18 | 2008-12-30 | Wm. Wrighley Jr. Company | Confection center fill apparatus and method |
DE102008014342A1 (en) * | 2008-03-14 | 2009-10-01 | Roga Kg | Method for the production of tube like foil by extrusion, comprises decelerating and then accelerating flow speed of a coextrudate within an extrusion nozzle |
GB201112475D0 (en) | 2011-07-20 | 2011-08-31 | Kritis Plastika | Concentric co-extrusion die |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3308508A (en) * | 1964-10-02 | 1967-03-14 | Dow Chemical Co | Die |
US3337914A (en) * | 1966-01-03 | 1967-08-29 | Nat Distillers Chem Corp | Stacked extrusion die |
FR2007073A1 (en) * | 1968-04-26 | 1970-01-02 | Northern Petro Chem Co | |
CA904525A (en) * | 1969-03-29 | 1972-07-11 | Leco Industries Limited | Co-extrusion device |
US3802826A (en) * | 1970-03-31 | 1974-04-09 | Nat Distillers Chem Corp | Rotatable co-extrusion die |
FR2234977A1 (en) * | 1973-06-27 | 1975-01-24 | Crown Zellerbach Corp | |
US3890083A (en) * | 1973-05-30 | 1975-06-17 | Leco Industries Ltd | Extrusion devices |
DE2752932A1 (en) * | 1977-11-26 | 1979-05-31 | Reifenhaeuser Kg | RING SPLITTING TOOL FOR EXTRUSION OF THERMOPLASTIC PLASTIC |
JPS5624133A (en) * | 1979-08-07 | 1981-03-07 | Asahi Chem Ind Co Ltd | Molding die |
EP0063060A1 (en) * | 1981-04-09 | 1982-10-20 | COMPAGNIE FRANCAISE DE RAFFINAGE Société anonyme dite: | Head for extruding a tubular parison having at least one layer of material |
EP0076366A2 (en) * | 1981-10-05 | 1983-04-13 | Ball Corporation | Multilayer tubular body with uncentered barrier layer |
GB2153739A (en) * | 1983-12-27 | 1985-08-29 | Toyo Seikan Kaisha Ltd | Process for production of multi-layer polyethylene terephthalate pipes for (stretch) blow moulding |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3026565A (en) * | 1961-01-04 | 1962-03-27 | Franklin Res And Dev Corp | Extruder head for hollow products |
FR2557016A2 (en) * | 1983-12-23 | 1985-06-28 | Raffinage Cie Francaise | HEAD FOR EXTRUSION OF A TUBULAR PARAISON TO AT LEAST ONE LAYER OF POLYMERIC MATERIAL |
-
1986
- 1986-01-18 DE DE19863601345 patent/DE3601345A1/en not_active Withdrawn
-
1987
- 1987-01-14 FI FI870132A patent/FI870132A/en not_active Application Discontinuation
- 1987-01-14 GB GB8700774A patent/GB2185931B/en not_active Expired
- 1987-01-15 SE SE8700129A patent/SE8700129L/en not_active Application Discontinuation
- 1987-01-15 NO NO870158A patent/NO870158L/en unknown
- 1987-01-16 IT IT19103/87A patent/IT1201161B/en active
- 1987-01-16 FR FR878700465A patent/FR2593112B1/en not_active Expired - Fee Related
- 1987-01-16 NL NL8700104A patent/NL8700104A/en not_active Application Discontinuation
- 1987-01-16 BE BE8700016A patent/BE1001610A4/en not_active IP Right Cessation
- 1987-01-16 DD DD87299296A patent/DD253216A5/en unknown
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3308508A (en) * | 1964-10-02 | 1967-03-14 | Dow Chemical Co | Die |
US3337914A (en) * | 1966-01-03 | 1967-08-29 | Nat Distillers Chem Corp | Stacked extrusion die |
FR2007073A1 (en) * | 1968-04-26 | 1970-01-02 | Northern Petro Chem Co | |
CA904525A (en) * | 1969-03-29 | 1972-07-11 | Leco Industries Limited | Co-extrusion device |
US3802826A (en) * | 1970-03-31 | 1974-04-09 | Nat Distillers Chem Corp | Rotatable co-extrusion die |
US3890083A (en) * | 1973-05-30 | 1975-06-17 | Leco Industries Ltd | Extrusion devices |
FR2234977A1 (en) * | 1973-06-27 | 1975-01-24 | Crown Zellerbach Corp | |
DE2752932A1 (en) * | 1977-11-26 | 1979-05-31 | Reifenhaeuser Kg | RING SPLITTING TOOL FOR EXTRUSION OF THERMOPLASTIC PLASTIC |
JPS5624133A (en) * | 1979-08-07 | 1981-03-07 | Asahi Chem Ind Co Ltd | Molding die |
EP0063060A1 (en) * | 1981-04-09 | 1982-10-20 | COMPAGNIE FRANCAISE DE RAFFINAGE Société anonyme dite: | Head for extruding a tubular parison having at least one layer of material |
EP0076366A2 (en) * | 1981-10-05 | 1983-04-13 | Ball Corporation | Multilayer tubular body with uncentered barrier layer |
GB2153739A (en) * | 1983-12-27 | 1985-08-29 | Toyo Seikan Kaisha Ltd | Process for production of multi-layer polyethylene terephthalate pipes for (stretch) blow moulding |
Non-Patent Citations (1)
Title |
---|
PATENT ABSTRACTS OF JAPAN, vol. 5, no. 72 (M-68)[744], 14 mai 1981; & JP-A-56 24 133 (ASAHI DOW K.K.) 07-03-1981 * |
Also Published As
Publication number | Publication date |
---|---|
FR2593112A1 (en) | 1987-07-24 |
IT1201161B (en) | 1989-01-27 |
FI870132A0 (en) | 1987-01-14 |
GB8700774D0 (en) | 1987-02-18 |
FR2593112B1 (en) | 1990-06-08 |
SE8700129D0 (en) | 1987-01-15 |
NO870158L (en) | 1987-07-20 |
GB2185931B (en) | 1989-11-01 |
NO870158D0 (en) | 1987-01-15 |
FI870132A (en) | 1987-07-19 |
NL8700104A (en) | 1987-08-17 |
SE8700129L (en) | 1987-07-19 |
DE3601345A1 (en) | 1987-07-23 |
GB2185931A (en) | 1987-08-05 |
DD253216A5 (en) | 1988-01-13 |
IT8719103A0 (en) | 1987-01-16 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
RE | Patent lapsed |
Owner name: REIFENHAUSER G.M.B.H. & CO. MASCHINENFABRIK Effective date: 19920131 |