CA1185761A - Coextrusion die - Google Patents

Coextrusion die

Info

Publication number
CA1185761A
CA1185761A CA000371885A CA371885A CA1185761A CA 1185761 A CA1185761 A CA 1185761A CA 000371885 A CA000371885 A CA 000371885A CA 371885 A CA371885 A CA 371885A CA 1185761 A CA1185761 A CA 1185761A
Authority
CA
Canada
Prior art keywords
die
extrusion die
passages
distribution
elements
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.)
Expired
Application number
CA000371885A
Other languages
French (fr)
Inventor
Ole-Bendt Rasmussen
BõRGE JENSEN
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Application granted granted Critical
Publication of CA1185761A publication Critical patent/CA1185761A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/49Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using two or more extruders to feed one die or nozzle
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/14Extrusion 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
    • B29C48/147Extrusion 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
    • B29C48/1472Extrusion 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/16Articles comprising two or more components, e.g. co-extruded layers
    • B29C48/18Articles comprising two or more components, e.g. co-extruded layers the components being layers
    • B29C48/21Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/32Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/32Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
    • B29C48/335Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles
    • B29C48/337Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles the components merging at a common location
    • B29C48/338Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles the components merging at a common location using a die with concentric parts, e.g. rings, cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2791/00Shaping characteristics in general
    • B29C2791/004Shaping under special conditions
    • B29C2791/007Using fluid under pressure

Abstract

Abstract of the Disclosure A coextrusion die for the extrusion of plastics materials in the shape of a tubular film comprising supply means for separately supplying at least two plastics materials to said die, a distribution channel system connected to each supply means, each distribution channel system comprising at least two arched channels provided in different axial planes, the ends of each arched channel being connect-ed to the middle portion of the following arched channel and the distribution channel systems being located at different distances from the centre axis of the die, collecting chambers communicating with said distribution channel systems and an annular extrusion slot com-municating with the collecting chambers.

Description

~576~

This invention relates to an extrusion die for the coextrusion of plastics materials in the form of a tubular film, said apparatus comprising means for separately supplying at least two extrudable materials in liquid state to said apparatus, a system of distribution channels connected to each supply means to form partial streams of said ext.rudable materials, each system of distribution channels opening into an annular collecting chamber, and an annular e~trusion slot communicating with said annular collecting chamber(s).
In a prior art coextrusion die of the above mentioned type each extrudable material is supplied in liquid state through a centrally located supply conduit which is connected to a system of rad.ially extending distribution channels, each system being provided in a distribution plate, and is then passed into an annular collecting chamber from which it is passed into a common annular extrusion slot.
Due to the presence of the radially e~tending distribu-tion channels in the prior art coextrusion there is insufficient space for the strong clamping bolts which are re~uired to maintain ~0 the distributîon plates sufficiently tensioned to avoid leakage of extrudable materials between sa.id plates at high e~trusion pressures.
The prior art supply system for extrudable materials com-prising centrally located supply conduits also suffer from the drawback that i.t allows no space at the centre of the die for the provision of driving means when it is desired to rotate the inner and outer die parts relative to one another or for the provision of supply and discharge conduits for gaseous coolant, such as air : 2 , ~

76~

to cool and expand the extruded tubular film. In the a~sence of such cooling, the production rate is considerably reduced.
The ob~ect of the invention is to provide a coextrusion die providing sufficient space for the provision o~ clamping bolts, means for rotating one of the die parts relative to one another and supply and discharge conduits for gaseous coolant.
According to the invention there is provided an extrusion die for the coextrusion of plural plastic materials into the form of a tubular film, said die comprising: A) means for separately supplying at least two extrudable plastic materials in a fluid state; B) a material distribution section comprising an array of annular elements providing a plurality of pairs of mutually con-tacting surfaces, at least one of said surfaces of each pair being recessed to define a labyrinthine distribution channel system for each such material, said system having an inlet opening connected to one o said supply means and dividing into opposite generally peripherally extending passages terminating in axially extending connecting passages which in turn divide into opposide peripherally extending passages terminating in axially extending connecting pass-ages which in turn divide into oppositely peripherally extending passages terminating in axially connecting passages, the number of said passage divisions being sufficient to provide an array of a-t least eight peripherally spaced apart connecting passages for each extrudable material opening generally axially through an end wall of said distribution sectionl the plural distribution channel systems being arranged in radially displaced relation a-t dif~erent radial distances ~rom the centre axis of the extrusion die; C~ an extrusion die section having one end wall contacting said distri-57~;~

bution section end wall and comprising a plurality of concentric generally annular elements having generally spaced parallel con-centric surfaces defining a plurality of continuous annular collec-ting chambers, one for each extrudable material, transition passage means communicating between the open ends of each array of said connecti~g passages from said distribution section and the interior end of the corresponding collecting chamber, a common continuous annular extrusion slot axially downstream of said collecting chambers and opening through the opposite end wall of said die section, and delivery passage means merging the ends of the collec-ting chambers to form a common interior end of said extrusion slot spaced upstream from said slot opening; and D) mechanical engage-ment means uniting the annular elements of said distribution and extrusion die sections, respectively, and connecting said sections together with said end faces in contact.
In the following the invention will be described with xe~erence to an extrusion die for the coextrusion of three extrud-able materials, wherein the generally peripherally extending pass-ages are circular arches and wherein the distribution channel systems are located concentrically ~ecause the use of such peripherally extending passages or distribution channels and the concentric mounting of these systems are particularly advantageous as far as the manufacture of the extrusion die is concerned.
However, it should be understood that the die may com-prise two or more than three distribution channel systems and that the peripherally extending passages or distribution channels should not necessarily ha~e the shape of circular arches and even may be composed of linear channel sections and that the distribution ~ ~S76~

channel systems do not have to be concentrically mounted.
The invention is based on the discovery that by effecting the distribution of each extrudable material in a labyrinthic manner as different distances from the centre axis of the die and in differen~ axial planes thereof, it is possible to prepare a tubular film coextruded of different plastics materials while avoiding the presence of conduits for supplying extrudable mater-ials to the die in the central zone of the die. Thus, the supply conduits can be connected to the end surface or exterior surface of the die and can be connected to the first peripherally extend-ing passage of each distribution channel system through connection channels provided in the die.
Thus, the necessary clamping bolts can be inserted between the distribution channel systems and and driving means, if any, for the rotation of the inner die part as well as conduits for gaseous coolant can be mounted in the central zone of the die.
By pxoviding the distribution channel systems at different distances from the centre axis of the die, it is also po~ssible to provide within the die drainage conduits for draining extruded material leaking from the distribution channels.
United States patent specification No. 3.698.988 discloses an extrusion die for the extrusion of a tubular film on a preformed tubular body. The prior art extrusion die which is no coextrusion die comprises a supply conduit for supplying a plastics material to a first arched distribution channel which is provided in a plate member. Each end of said first distribution channel is connected to a second arched distribution channel provided in an adjacent plate.

S~6~L

The ends of said latter distribution channel are con-nected to an annular inner distri~ution channel provided within the same plate and having a diameter which is less than that of the first and second distribution channels. Thus, the flow of material from said arched distribution channels to said annular distribution channel which opens into an annular extrusion die is a radial flow and not an axial flow.
United States Patent 2,820,249 Colombo discloses an apparatus for applying an e~terior multi-layer polymeric or resin coating onto steel pipe or the like, and shows an extrusion die which utili~es labyrinthine distribution channel systems. These channel systems are necessarily spaced radially from the axis of the die inasmuch as the pipe must pass through the hollow centre of the die for coating. The respective distribution systems are at different radial distances from the die axis and terminate in passag~s directed radially. Thus the Colombo die cannot achieve the basic effect of the coe~trusion die of the present invention, namely forming a tubular film of uniformly distributed coextruded plastics materials.
The part of the extrusion die of the invention in which the pexipherally extending passages or distribution channels are provided preferably consists of elements which are clamped together and the channels are preferably formed from grooves provided in the surfaces of said elements~
An extrusion die composed of such elements presents several advantages as far as its manufacture is concerned. Thus~
it is much simpler to form grooves in the surface of such elements than to form internal channels therein. Furthermore, it is easy to 5a ,,~, i ~IL857~3~

maintain and clean such a die because the elements can easily be replaced, and when the die has been disassembled the grooves form-ing the distribution channels are easily cleaned.
The distribution channels and the connecting passages or channels connecting the ends of one distribution channel with the middle portions of the following ones may have any cross-sectional shape. In practice, however, it has been found preferable to use channels having an essentially rectangular cross-sectional shape with rounded corners in order to obtain uniform flow and to prevent thermal conversion of slowly flowing materialO
An embodiment of the extrusion die of the invention com-prises distribution channels each formed from two grooves, one groove being formed in the surface of one element and the other in the surface of the adjacent element. This embodiment is partic-ularly advantageous because it allows distribution channels having circular cross-section or having rounded corners to be formed in a simple manner.
In another preferred embodiment of the die of the inven-tion the elements are disc-shaped and the distribution channels ~0 are interconnected through connecting passages extending through the intermediate discs. Such disc-shaped elements are particularly preferred because they can be clamped together to form distribution channels without dead zones, even if the elements are warped eOg.
as a result of a high temperature cleaning of the distribution channels.
The elements are preferably discs which extend perpendi-cular to the axis of the extrusion die and in that case the con-necting channels preferably are parallel to said axis~

5b 576~

The portion of the extrusion die comprising the distri-bution channel system may also be composed of shell-shaped elements inserted in one another and the connecting channels are preferably formed from grooves formed in the surfaces of the shell-shaped elements. Such a die is easily manufactured because all passages of the distribution channel system can be ~ormed by cutting.
A particularly uniform distribution of the extrudable material in the annular collecting chambers can be achieved by providing guide grooves at the points where the distribution channels open into the collecting chamb~rs, said guide grooves being inclined relative to the centre a~is of the die and the depth of said grooves gradually decreasing in the longitudinal direction of the die.
Due to the presence of said guide grooves the extrudable materials are subjected to a transverse movement after passing into the collecting chambers and said trans~erse movement contributes to the elimination or reduction of irregularities in the tubular bodies formed in the collecting chambers.
A similar effect is achieved by using an extrusion die in which at least one chamber wall in each collecting chamber is rotatable relative to the openings through which the distribution channels open into the collecting chamber considered.
The number and the length of the distribution channels are preferably selected such that the channels through which a given distribution channel system is connected to a collecting chamber is unifo~mly distributed over the periphery of the collec-ting chamber. In this manner the extrudable material supplied to said collecting chamber is uniformly di~tributed over the whole periphery of the tubular film formed in the ~xtrusion slot.
The invention will now be described in further detail with ` ~ 5d ~5~
reference to the drawings in which Fig. 1 is a diagrammatic perspective view of an embodi-ment of an extrusion die according -to the inven-tion fed by three extruders, Fig. 2 is a longitudinai sectional view oF the extrusion die oF Fig . 1 taken aiong the line l l - I l, Fig. 3 is a part of the distribution channel system of the extrusion die of Fig. 2 shown in unfolded view, and Fig. ~ is a longitudinal sectional view oF part of another embodiment of the extrusion die accordin0 to the i nvention .
Fig. 1 illustrates a coextrusion die 1 which through supply conduits is fed by three extruders 3. Each extruder 3 comprises a supply funnel 4 for extrudable material. The ex~rusion die 1 has an 15 annular extrusion siot 5 For the extrusion of a tubular film 6.
Figs. 2 and 3 shows -the extrusion die of Fig. 1 in enlarged scale. The supply conduit 2 which has one end inserted in a hole 10 in the end of the extrusis)n die 1 communiçates with the middle of the three distribution channel systems through a channel 11. The rear 20 end of the extrusion die to which the extrudable materials is fed is composed of plate elements 12-15 which are clamped together and which are attached to the front 0nd 16 of th~3 extrusion die by clamp-lng bolts 17 which are screwed into holes in said front end 16. Three collecting chambers 18-20 are provided in said front end, one end of 25 each collecting chamber communicating wi-th a distribution channel system and the opposite ends of said collecting chambers 18-20 being connected to the annular extrusion slot 5.
The location of the extrusion slot 5 and consequently the thickness of the extruded tubular film is adjustable by means of ad-30 justing screws 21 and 22.
In the embodiment illustrated in Fig. 2 the extrusion die is providecl with electric heating jackets 23 on both the exterior and interior surfaces thereof.
The three distribution channel systems are in principle 35 identical and only the middle system will be described with reference fo Fig. 3.

~57G~

The channel 11 connecting the supply conduit Z with the distribution channel system opens into the middle portlon of a first arched distribution channel 24. Each end of said channel is connected -to the middle portion of a group of arched dis-tribution channels 25.
The ends of said channels 25 are in turn connected to the middle 5portion of another group of arched distribution channels 26. The ends of the dis-tribution channels are connected to the collecting chamber 19 through connecting channels 27.
In order to obtain a good distribution of the partial streams leaving the channeis 27, guide grooves are provided in the wall oF
10the collecting chamber 19, said guide grooves 27 being inclined rela-tive to the longitudinal axis of the die and having a depth which gradually decreases.
The extrusion die illustrated in Fig. 4 consists of a sta-tionary part shown generally as 30, two rotatable parts 31 and 32 and 15located between parts 31 and 32 three collec~ing chambers 33, 34 and 35, each being connected to an annular extrusion slot 36.
The rotatable part 32 is mounted on a central shaft 37 cooperatin3 with driving means (not shown) mounted in a central bore in the stationary part 30 of the die. The exterior surface of the rotatable part 31 has the shape of a toothed wheel which is in engage-ment with a pinion (not shown).
A guide ring 39 with a washer 40 attached to the stationary part 30 is inserted in an annular guide groove 4'1 in the rotatable part 32. Similarly a guide ring 42 with washer 43 which are also 25attached to the s~ationary part 30 are inserted in an annular guide groove 44 in the rotatable part 31.
The distribution channel system of the die illustrated in Fig. 4 corresponds to that of Figs. 2 and 3 but the arched distri-bution channels Z4, 25 and 26 are composed of grooves which are 30provided in the conical surfaces of an inner element 45 and two sur-rounding conical shells 46 and 47 as well as an outer shell 48 which has a conical inner surface, and a channel 49 connecting a supply conduit 2 with the first arched channel 24.
Th~3 elements 45-48 containing the distribution channel 35system are clamped together by a plate 51 comprising a set of holes 50 and bolts 52 which are inserted in said holes 50 and attached to ~57~
`- the elements ~5-~8. Due to the conical shape of the contact surfaces of the elements 45-48 onlv a small force and consequently relatively thin and shor-t bolts are required to clamp together the portions Forming the sta-lionary part oi~ the die.
The space between the outer rotatable part 31 and the in-ner rotatable part 32 comprises two elements 53,54 oF which one 53 by means of fastening means (not shown) having a small cross-sect70nal area is connected to -the rotatable part 31 and the second one 54 by means of similar fastening means (not shown) is connected to the other rotatable part 32.
When using the embodiment of the die illustrated in Fis3s. 2 and 3, the streams flowing out of the channels 27 are smeared out during the passage through the zone in which the guide grooves 28 are provided.
In the embodiment illustrated in Fig. 4 the streams are 15 smearecl out as a result of the movement o-f the rotatable parts 31, 32. These parts can be rotated in opposite directions (contrarotated) or in the same direction a~ different or equal speeds of rotation.
Alternatively, one part can be rotated whi~e the other part is station-ary .
It should be understood that the embodiment illustrated in Figs. 2 and 3 also might comprise rotatable die parts and that guide grooves also rnight be provided in walls oF the collecting chambers illustrated in Flg. 4.
The ernbodiments of the extrusion die shown in the draw-25 ings are designed for the manufacture of laminates consisting of three layers located parallei to the surFaces of the laminates. However, if the extrusion die shown is modified such that one or t~o distribution channels systems open into the sarne collecting chamber, products could be manufactured wherein segments of the extrudable materials 30 are located side by side in one or more layers or extending from one surface to the opposite. Such a modified embodiment of the extrusion die according to the invention would be suitable for the manufacture of products of the type disclosed in US patent specifications Nos.
3.565.744, 3.505.162, 3.632.2~2 and 3.690.982 and part of the extru-35 sion die of the invention which comprises the distribution channel system could be combined with the apparatus described in said US
patent specifications.

Claims (8)

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. An extrusion die for the coextrusion of plural plastic materials into the form of a tubular film, said die comprising:
A) means for separately supplying at least two extrud-able plastic materials in a fluid state;
B) a material distribution section comprising an array of annular elements providing a plurality of pairs of mutually contacting surfaces, at least one of said surfaces of each pair being recessed to define a labyrinthine distribution channel system for each such material, said system having an inlet opening con-nected to one of said supply means and dividing into opposite generally peripherally extending passages terminating in axially extending connecting passages which in turn divide into opposite peripherally extending passages terminating in axially extending connecting passages which in turn divide into oppositely peripheral-ly extending passages terminating in axially connecting passages, the number of said passage divisions being sufficient to provide an array of at least eight peripherally spaced apart connecting passages for each extrudable material opening generally axially through an end wall of said distribution section, the plural dis-tribution channel systems being arranged in radially displaced relation at different radial distances from the centre axis of the extrusion die;
C) an extrusion die section having one end wall contact-ing said distribution section end wall and comprising a plurality of concentric generally annular elements having generally spaced parallel concentric surfaces defining a plurality of continuous annular collecting chambers, one for each extrudable material, transition passage means communicating between the open ends of each array of said connecting passages from said distribution section and the interior end of the corresponding collecting chamber, a common continuous annular extrusion slot axially down-stream of said collecting chambers and opening through the opposite end wall of said die section, and delivery passage means merging the ends of the collecting chambers to form a common interior end of said extrusion slot spaced upstream from said slot opening; and D) mechanical engagement means uniting the annular elements of said distribution and extrusion die sections, respec-tively, and connecting said sections together with said end faces in contact.
2. An extrusion die as in claim 1, characterized in that the distribution channel systems are disposed in concentric relationship.
3. An extrusion die as in claim 1, characterized in that said distribution section is composed of annular elements which are clamped together, and that both surfaces of said elements are recessed to define said passages.
4. An extrusion die as in claim 3, characterized in that the elements are disc-shaped and that the axial passages extend through the intervening disc-shaped elements while said peripheral passages are formed in at least one face thereof.
5. An extrusion die as in claim 3, characterized in that said part of the die comprises annular frusto-conical elements nestled together and that the distribution passages are formed from recesses provided in at least one surface of said frusto-conical elements.
6. The extrusion die of claim 1, wherein said transition passage means is of gradually decreased radial depth and gradually increasing peripheral width relative to said opening in said distribution section end face.
7. The extrusion die of claim 6, wherein the change in shape of said transition passages is generally asymmetrical.
8. The extrusion die of claim 6, wherein each transition passage includes an inclined groove extending into the correspond-ing collecting chamber.
CA000371885A 1980-02-29 1981-02-27 Coextrusion die Expired CA1185761A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DK89180A DK146217C (en) 1980-02-29 1980-02-29 coextrusion die
DK891/80 1980-02-29

Publications (1)

Publication Number Publication Date
CA1185761A true CA1185761A (en) 1985-04-23

Family

ID=8098701

Family Applications (1)

Application Number Title Priority Date Filing Date
CA000371885A Expired CA1185761A (en) 1980-02-29 1981-02-27 Coextrusion die

Country Status (21)

Country Link
US (2) US4403934A (en)
EP (2) EP0092188B1 (en)
JP (1) JPS6365013B2 (en)
AT (1) ATE57651T1 (en)
AU (1) AU551951B2 (en)
BE (1) BE887724A (en)
BR (1) BR8107091A (en)
CA (1) CA1185761A (en)
DE (1) DE3177225D1 (en)
DK (1) DK146217C (en)
ES (1) ES499877A0 (en)
FI (1) FI80850C (en)
GR (1) GR74093B (en)
IE (1) IE56626B1 (en)
IL (1) IL62224A (en)
IT (1) IT1138963B (en)
MX (1) MX154582A (en)
PT (1) PT72589B (en)
SU (1) SU1371494A3 (en)
WO (1) WO1981002406A1 (en)
ZA (1) ZA811294B (en)

Families Citing this family (52)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK146217C (en) * 1980-02-29 1984-03-05 Rasmussen O B coextrusion die
US4784594A (en) * 1983-03-11 1988-11-15 Mobil Oil Corporation Single lip rotary tubular extrusion die
US6129960A (en) 1983-04-13 2000-10-10 Pechiney Plastic Packaging, Inc. Methods and apparatus for injection molding and injection blow molding multi-layer plastic and the articles made thereby
US4511528A (en) * 1983-04-13 1985-04-16 American Can Company Flow stream channel splitter devices for multi-coinjection nozzle injection molding machines
US4946365A (en) * 1983-04-13 1990-08-07 American National Can Company Apparatus for injection molding and injection blow molding multi-layer articles
US4892699A (en) * 1983-04-13 1990-01-09 American National Can Company Methods for injection molding and injection blow molding multi-layer articles
US5037285A (en) 1983-04-13 1991-08-06 American National Can Company Apparatus for injection molding and injection blow molding multi-layer articles
US5523045A (en) 1983-04-13 1996-06-04 American National Can Company Methods for injection molding and blow-molding multi-layer plastic articles
FI67674C (en) * 1984-02-24 1985-05-10 Nokia Oy Ab DOUBLE EXTRUDER FOR FRAME EXAMINATION OF EXTERNAL PRODUCTS
US4748031A (en) * 1985-04-17 1988-05-31 Nabisco Brands, Inc. Method of triple co-extruding bakeable products
US4715803A (en) * 1985-04-17 1987-12-29 Nabisco Brands, Inc. Triple co-extruder
US4765999A (en) * 1985-07-26 1988-08-23 Presto Products, Incorporated Polyester/copolyester coextruded packaging film
DE3534770C1 (en) * 1985-09-30 1986-11-13 Hermann Berstorff Maschinenbau Gmbh, 3000 Hannover Method and arrangement for starting up a multiple extrusion press with little loss of material in order to produce profile sections made of different rubber or plastic mixtures, for example for treads or side strips of vehicle tires
US4716061A (en) * 1985-12-17 1987-12-29 Presto Products, Incorporated Polypropylene/polyester nonoriented heat sealable moisture barrier film and bag
US4705707A (en) * 1985-12-17 1987-11-10 Presto Products, Incorporated Polyethylene/polyester nonoriented heat sealable moisture barrier film and bag
US4946743A (en) * 1987-06-26 1990-08-07 Reynolds Consumer Products, Inc. Nonoriented polyester films for lidding stock with modified heat seal layer
AT387672B (en) * 1987-08-12 1989-02-27 Rosendahl Masch Gmbh DEVICE FOR INJECTING A SOUL, IN PARTICULAR AN ELECTRIC LADDER
US5102323A (en) * 1988-08-31 1992-04-07 American National Can Company Plastic resin multi-layer co-extrusion extruder with multi-port plug for selecting order of layers
US5297946A (en) * 1989-07-21 1994-03-29 The Japan Steel Works, Ltd. Multilayer parison extruder
US5110276A (en) * 1989-12-28 1992-05-05 Farnsworth John T Extrusion die assembly
DE4020819A1 (en) * 1990-06-29 1990-11-08 Bock Stefan Dipl Ing Fh STORAGE HEAD FOR THE PRODUCTION OF SINGLE OR MULTILAYER HOSE-OVER-HOSE STRUCTURED PREFORMS FROM THERMOPLASTICS
CA2082437C (en) * 1991-11-14 1998-01-20 Peter C. Gates Spiral fed multi-layer tubular die
NL9201457A (en) * 1992-08-14 1994-03-01 Rollepaal B V Maschf De Dividing head for forming a tubular profile from one or more streams of extruded thermoplastic plastic material.
WO1996033856A1 (en) * 1995-04-24 1996-10-31 Black Clawson Sano Inc. Extrusion die
US6190152B1 (en) * 1996-08-26 2001-02-20 Addex, Inc. Regular division of molten extrusion flow
US6245401B1 (en) 1999-03-12 2001-06-12 Kimberly-Clark Worldwide, Inc. Segmented conformable breathable films
IT1313342B1 (en) * 1999-08-03 2002-07-23 Macchi S R L EXTRUSION HEAD FOR MULTILAYER PLASTIC FILMS.
US7648658B2 (en) * 2000-02-04 2010-01-19 Harrel, Inc. Alternate polymer extrusion method with reduced drool
US6343919B1 (en) * 2000-02-28 2002-02-05 Ricardo Pablo Rodriguez Modular plastics extrusion die
GB0114691D0 (en) 2001-06-15 2001-08-08 Rasmussen O B Laminates of films and methods and apparatus for their manufacture
US6682333B2 (en) 2001-10-25 2004-01-27 Extrusion Dies Industries Llc Quick-release extrusion die
PT1480815E (en) * 2002-03-04 2007-01-31 Rasmussen Ole-Bendt Crosslaminate of oriented films, method of manufacturing same, and coextrusion die suitable in the process
CN100339211C (en) * 2002-12-13 2007-09-26 奥利-本特·拉斯马森 Laminates of films having improved resistance to bending in all directions and methods and apparatus for their manufacture
RU2349454C2 (en) * 2003-04-24 2009-03-20 РАСМУССЕН Оле-Бентг Method for manufacturing of oriented film from thermoplastic polymer alloys, device for film manufacture and manufactured goods
US7678316B2 (en) * 2004-06-08 2010-03-16 3M Innovative Properties Company Coextruded profiled webs
GB0424355D0 (en) * 2004-11-03 2004-12-08 Rasmussen O B Improved method of manufacturing an alloyed film apparatus for the method and resultant products
GB0426839D0 (en) * 2004-12-07 2005-01-12 Rasmussen O B Small container made from thermoplastic sheet material
US7897081B2 (en) * 2004-12-30 2011-03-01 3M Innovative Properties Company Method of extruding articles
ATE550183T1 (en) 2005-01-07 2012-04-15 Ole-Bendt Rasmussen LAMINATE MADE OF THERMOPLASTIC FILM MATERIALS HAVING CONTINUOUS POROSITY AND METHOD FOR FORMING IT
DE602006005148D1 (en) 2005-04-08 2009-03-26 Ole-Bendt Rasmussen METHOD AND DEVICE FOR FOLLOWING EXTRUSION
RU2490126C2 (en) 2005-05-11 2013-08-20 Оле-Бентт РАСМУССЕН Cross laminar plastic from oriented films and method and device for its fabrication
US7513766B2 (en) * 2005-10-11 2009-04-07 Cryovac, Inc. Extrusion apparatus having a driven feed segment
US8034431B2 (en) * 2006-01-25 2011-10-11 3M Innovative Properties Company Intermittently bonded fibrous web laminate
US7622180B2 (en) * 2006-07-10 2009-11-24 3M Innovative Properties Company Net hook fasteners
TWI499497B (en) 2008-01-17 2015-09-11 Ole-Bendt Rasmussen Film material exhibiting textile properties, and method and apparatus for its manufacture
GB0814308D0 (en) * 2008-08-05 2008-09-10 Rasmussen O B Film material exhibiting textile properties, and method and apparatus for its manufacture
RU2448831C2 (en) * 2011-03-09 2012-04-27 Алексей Николаевич Докукин Extrusion line for producing flat thread from synthetic raw stock
RU2447995C2 (en) * 2011-03-09 2012-04-20 Алексей Николаевич Докукин Method of extruding flat thread from synthetic raw stock
JP6039845B1 (en) * 2016-03-30 2016-12-07 株式会社湘南貿易 Inflation film forming die
US20180187802A1 (en) * 2016-12-30 2018-07-05 Polyflow Llc Multi-layer pipes
US20210079562A1 (en) 2017-12-21 2021-03-18 Beaulieu International Group Nv Biodegradable fabric and use of such fabric
US20210402668A1 (en) * 2018-09-27 2021-12-30 Vanderbilt University Multi-material printing device for energy storage and conversion applications

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2734224A (en) * 1956-02-14 winstead
FR1084310A (en) * 1952-06-17 1955-01-18 Lavorazione Mat Plastiche Sas Extrusion head for multi-coated cables
CH315684A (en) * 1952-10-08 1956-08-31 Lavorazione Mat Plastiche Sas Protective coating for metal pipes, process for its manufacture and apparatus for carrying out this process
FR1432131A (en) * 1965-04-22 1966-03-18 Barmag Barmer Maschf Offset injection head for extruders
US3418687A (en) * 1966-10-24 1968-12-31 Du Pont Extruding apparatus
US3475789A (en) * 1968-01-16 1969-11-04 Nrm Corp Blown film dies
US3649143A (en) * 1969-05-01 1972-03-14 Pierson Ind Inc Composite tubular film apparatus
US3756758A (en) * 1969-07-15 1973-09-04 Chemplex Co Extrusion die for plastic film
DE1953114A1 (en) * 1969-10-22 1971-05-06 Barmag Barmer Maschf Multi-layer tube extrusion head
FR2136960B1 (en) * 1971-05-10 1973-05-11 Fayet Andre
US3809515A (en) * 1972-03-03 1974-05-07 Farrell Patent Co Extrusion die for blowing plastic film
US3947173A (en) * 1972-09-13 1976-03-30 Western Electric Company, Inc. Apparatus for extruding concentric plastic sheaths
GB1384979A (en) * 1973-04-05 1975-02-26 Farrell J J Extrusion die for blowing plastic film
US3890083A (en) * 1973-05-30 1975-06-17 Leco Industries Ltd Extrusion devices
US4039364A (en) * 1974-07-05 1977-08-02 Rasmussen O B Method for producing a laminated high strength sheet
GB1526722A (en) * 1974-07-05 1978-09-27 Rasmussen O Method for producing a laminated high strength sheet
US4017240A (en) * 1975-11-19 1977-04-12 Rubbermaid Incorporated Die for extruding sheet material
JPS5369264A (en) * 1976-12-03 1978-06-20 Purasuchitsuku Kougaku Kenkiyu Multiilayer circular die
JPS5431465A (en) * 1977-08-16 1979-03-08 Kureha Chem Ind Co Ltd Die for extruding multilayered tube
US4185954A (en) * 1977-08-23 1980-01-29 Kabushiki Kaisha Plastic Kogaku Kenkyusho Die for extruding tubes composed of a plurality of layers
US4182603A (en) * 1978-03-27 1980-01-08 Egan Machinery Company Multilayer tubular extrusion die
US4268239A (en) * 1978-05-30 1981-05-19 Mobil Oil Corporation Tubular extrusion die
US4201532A (en) * 1978-08-02 1980-05-06 Cole Robert J Extrusion dies of spiral mandrel type
DK146217C (en) * 1980-02-29 1984-03-05 Rasmussen O B coextrusion die

Also Published As

Publication number Publication date
DK146217B (en) 1983-08-01
PT72589B (en) 1982-03-12
BE887724A (en) 1981-06-15
MX154582A (en) 1987-10-07
US4492549A (en) 1985-01-08
BR8107091A (en) 1982-01-05
SU1371494A3 (en) 1988-01-30
FI80850B (en) 1990-04-30
IE56626B1 (en) 1991-10-23
AU551951B2 (en) 1986-05-15
AU6788881A (en) 1981-09-11
ATE57651T1 (en) 1990-11-15
FI813344L (en) 1981-10-26
WO1981002406A1 (en) 1981-09-03
IE810378L (en) 1981-08-29
PT72589A (en) 1981-03-01
JPS57500374A (en) 1982-03-04
ES8301749A1 (en) 1982-12-16
US4403934A (en) 1983-09-13
EP0092188A2 (en) 1983-10-26
DE3177225D1 (en) 1990-11-29
FI80850C (en) 1990-08-10
EP0046789B1 (en) 1984-11-28
EP0092188A3 (en) 1985-10-02
JPS6365013B2 (en) 1988-12-14
IT8120028A0 (en) 1981-02-27
EP0092188B1 (en) 1990-10-24
DK89180A (en) 1981-08-30
ZA811294B (en) 1982-03-31
ES499877A0 (en) 1982-12-16
IL62224A (en) 1985-08-30
DK146217C (en) 1984-03-05
EP0046789A1 (en) 1982-03-10
IT1138963B (en) 1986-09-17
GR74093B (en) 1984-06-06

Similar Documents

Publication Publication Date Title
CA1185761A (en) Coextrusion die
JP4165660B2 (en) Modular disk coextrusion die
US20040070105A1 (en) Methods and apparatus for extruding a tubular film
KR100188402B1 (en) Method and apparatus for forming an article with multi-cellular densities and geometries
US5762971A (en) Modular disk coextrusion die
US4564350A (en) Plastic extruder assembly
CA1203961A (en) Twin-nozzle extrusion head
CA2373737C (en) Pipe extrusion die for multi-layer pipe
KR20120036968A (en) Die tooling for extruding tubular product
WO1995016553A9 (en) Symmetrical flow extrusion manifold
EP0683720A1 (en) Symmetrical flow extrusion manifold
JP3500414B2 (en) Distributor head for forming a tubular profile from a stream of one or more extruded thermoplastic materials
WO1996036475A9 (en) A tubular calibration unit for machines for extruding plastic strings such as pipes
US3461495A (en) Pelletizing die plate
US3762692A (en) Screw extruder for thermoplastic melts with temperature equalizing head
US4268239A (en) Tubular extrusion die
CA2541650A1 (en) Modules for c0-extrusion dies
GB9924160D0 (en) Continuous extrusion apparatus
EP0122703B1 (en) Single lip rotary die
WO2003033238A1 (en) Improved circumferential distribution in a circular extrusion die
EP1345749B1 (en) Methods and apparatus for extruding a tubular film
AU2002215035A1 (en) Methods and apparatus for extruding a tubular film
MXNL01000002A (en) Die for co-extrusion of blown film.

Legal Events

Date Code Title Description
MKEX Expiry