WO1990005626A1 - A method for manufacturing an elongated member and apparatus for carrying out the method - Google Patents

A method for manufacturing an elongated member and apparatus for carrying out the method Download PDF

Info

Publication number
WO1990005626A1
WO1990005626A1 PCT/SE1989/000652 SE8900652W WO9005626A1 WO 1990005626 A1 WO1990005626 A1 WO 1990005626A1 SE 8900652 W SE8900652 W SE 8900652W WO 9005626 A1 WO9005626 A1 WO 9005626A1
Authority
WO
WIPO (PCT)
Prior art keywords
matrix
compression
mixture
feeder
plastics material
Prior art date
Application number
PCT/SE1989/000652
Other languages
French (fr)
Inventor
Curt Andersson
Original Assignee
Curt Andersson
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
Priority claimed from SE8804156A external-priority patent/SE8804156L/en
Priority claimed from SE8901782A external-priority patent/SE8901782L/en
Application filed by Curt Andersson filed Critical Curt Andersson
Publication of WO1990005626A1 publication Critical patent/WO1990005626A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B11/00Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
    • B30B11/22Extrusion presses; Dies therefor
    • B30B11/24Extrusion presses; Dies therefor using screws or worms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B27WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27NMANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N3/00Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/08Moulding or pressing
    • B27N3/28Moulding or pressing characterised by using extrusion presses
    • 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
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/38Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in the same barrel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/39Plasticisers, homogenisers or feeders comprising two or more stages a first extruder feeding the melt into an intermediate location of a second extruder
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/625Screws characterised by the ratio of the threaded length of the screw to its outside diameter [L/D ratio]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/68Barrels or cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B11/00Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
    • B30B11/22Extrusion presses; Dies therefor
    • B30B11/224Extrusion chambers
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts

Definitions

  • TITLE OF THE INVENTION A method for manufacturing an elongated member and apparatus for carrying out the method
  • the present invention relates primarily to a method of manufacturing an elongated member, and in particular to a method in the continuous manufacture of an elon ⁇ gated member from a compressible and compressed start ⁇ ing material.
  • the invention also relates to apparatus for the con ⁇ tinuous manufacture of an elongated member with the use of compressible starting material.
  • the invention also relates to the use of a plastics material, particularly a plastics-material mixture as the compressible material.
  • the elongated member is produced from separate, well-defined batches which are mutually separated by an interface or boundary region of mutually different degrees of compression and in which the fibre directions are also displaced relative to one another, to a certain extent, in the vertical plane. Hardening takes place in a heating section.
  • Swedish Patent Application 8804156-1 describes a method and apparatus for manufacturing an elongated member from a mixture of a plastics material and a filler, such as wood fibres, textile fibres and the like, by compacting the mixture when the plastics material is in a molten state.
  • 15 energy generated by compression is utilized to soften and/or to melt the plastic content of the mixture, at least at the end of the compression section.
  • a particularly challenging technical problem also ari ⁇ ses in realizing that the aforesaid technical problems can be solved when the plastic content of the starting mixture is precompacted in a molten or heated state, 3.0 and is then caused to solidify in a cooling section.
  • the starting material may comprise waste material, where plastic material is of significance, and of realizing that the plastic mate ⁇ rial and filler should be mixed in appropriate propor ⁇ tions, particularly when the filler is a finely divided fibrous material r such as wood-fibre material, so as to obtain a mechanically strong elongated member.
  • a particularly challenging technical problem also ari ⁇ ses in the ability to realize the possibility that when the filler comprises a wood-fibre material, such as wood chips (sawdust , cutter chips) , and has been heat- dried in a preceding operation, the filler can be mixed with plastic material immediately after being dried, and the mixture further heated, when necessary, so as to convert the plastic content of the mixture to a tacky or liquid state, prior to compacting the mixture and subsequent cooling thereof to form said elongated member.
  • a wood-fibre material such as wood chips (sawdust , cutter chips)
  • the present invention relates primarily to a method of manufacturing conti ⁇ nuously an elongated member from compressible and com ⁇ pacted material.
  • the compressible material used comprises a mixture of plastics material and filler, and the mixture with its plastic content preferably in a molten state, is deli ⁇ vered to a first space and compacted therein.
  • the com ⁇ pressed material is then pressed into another space, defined by a matrix mould, where the mixture is cooled so that the plastic content thereof will solidify.
  • the thermal energy generated during compression of the mixture is adapted so that the temperature of the plastic material will be sufficiently high to soften, preferably melt said material.
  • the mixture is compressed with the aid of a screw-feeder, by controlling the speed of the screw- feeder and/or providing the helix of the screw-feeder with a pitch which decreases towards the aforesaid second space, so as to achieve desired compression within the screw-feeder.
  • the mixture can be precompressed with the aid of a further screw-feeder, but preferably at different rotational speeds.
  • the further screw-feeder will preferably rotate at a higher speed than the first mentioned screw-feeder.
  • precompression screw-fee ⁇ der will be stationary in relation to one of the sec ⁇ tions of said matrix, namely one end-part of the upper matrix-section.
  • the plastic content of the plastic-material/filler mixture comprises bet ⁇ ween 20 and 60%, say between 30-50%, normally about 40% of the total material content.
  • the filler used is preferably a newly dried and heated fibrous material, whereas the plastics material used may be waste-plastic, domestic plastic waste or some like inexpensive material.
  • Means are preferably provided for cooling the part of the matrix located adjacent the extruder, preferably with the aid of water.
  • the matrix is divided into sections, which are capable of being displaced synchronously or asynch ⁇ ronously in relation to one another, along the outer surfaces of the elongated member during the manufacture thereof.
  • the invention also relates to an apparatus for the continuous manufacture of an elongated member, this apparatus comprising a compression device having a rotatable shaft arranged concentrically with a matrix mould, and being operative to press the mixture through the matrix.
  • the apparatus also includes a preco pressing device which delivers precompressed mixture to the compressing device.
  • the matrix sections embrace the elongated member during its manufacture, and one or more of the matrix sections are reciprocatingly movable.
  • the precompressing device coacts with one section.
  • the elongated member can be used as a nailing batten, in the manufacture of door and window frames or like structures, or can be cut into given, short lengths for use in the manufacture of loading pallets.
  • Figure 1 is a side view, partially in section, of a first apparatus constructed in accordance with the invention
  • Figure 2 is a simplified sectional view taken on the line II-II i Figure 1;
  • Figure 3 is a side view of a second embodiment of the inventive apparatus, which incorporates a compression section in the form of an extruder; and
  • Figure 4 illustrates schematically a nozzle mounted on the extruder and capable of being connected to a matrix, not shown in detail.
  • the reference 1 in Figure 1 identifies a known appara ⁇ tus with which a plastics material can be mixed with a filler and/or a reinforcing material.
  • the apparatus shall be capable of enabling the plastics material to be heated and brought preferably to a mol ⁇ ten state, and in all events, to a tacky state.
  • the proportion of plastics mate ⁇ rial contained in the mixture will be less than 50% and preferably about 10%.
  • the normal value in this respect will preferably lie between 20 and 50%, say about 40%.
  • the apparatus 1 includes precompressing device in the form of a screw conveyor, by means of which a mixture A of plastics material and filler is fed to a first space 3, through a passage 2.
  • the chamber 3 is conceived to be defined by the conically tapering shaft 4 and helix 8 of a further screw conveyor and also a tubular matrix 5 which embraces said conveyor.
  • the material A When leaving the pas ⁇ sage 2, the material A exhibits a degree of precompre- ssion which is commensurate with the pressure exerted on the mixture as it moves through the passage 2.
  • the mixture A is then compressed successively to a much greater degree of compression by the screw-conveyor and tubular matrix 5, and at a region referenced B down ⁇ stream of the first space 3 the plastics material pre- sent in the mixture will be either in a molten or a tacky state.
  • the pla ⁇ - tics material solidifies gradually and when the mixture has reached the position referenced C, it is assumed that the plastics material, and thus also the elongated member, will be essentially solid, and that in all events the plastic/filler mixture will have been com- pressed to its final degree of compression when it rea ⁇ ches the region of the apparatus referenced D, so as to form a finished elongated member or organ.
  • the precompressed plastic/filler mixture is moved by means of the screw-feeder 4,8 from the region B, where the plastic material begins to solidify, through the tubular matrix 5 and into the beginning of a third space 7. Compression of the mixture during its travel from region A to region B is effected with the aid of the screw-feeder 4, 8.
  • he helix 8 of the screw-feeder has a pitch which decreases in a direction towards the third space 7, thereby providing the advantage that the mix ⁇ ture can be caused to have a predetermined degree of compression by the time it reaches the region B, due to t e successive decrease in the pitch of the helix 8.
  • the screw-feeder comprising the conically tapering shaft 4 and helix 8, is rotated by means of drive means not shown.
  • Figure 2 is a cross-sectional view which illustrates a matrix of rectangular cross-section divi- ded into four sections 5a, 5b, 5c and 5d.
  • Each of these matrix sections is intended to coact with a hydraulic piston-cylinder device 15, the piston of which is reciprocatingly movable in the direction of the longitudinal axis of the elongated member 10.
  • the different matrix sections can either be moved synchro ⁇ nously or asynchronously.
  • the matrix section 5a and 5c are held in position with the aid of rollers 16, 17, which extend along the whole length of the matrix 5 and which are present'in numbers that will ensure that the rollers fullfil the function satisfactorily.
  • the matrix sections 5b and 5d are also held in position with the aid of -rollers, although not shown.
  • cooling passages are provided in the matrix sections 5a, 5b, 5c and 5d in a manner known per se. so that heat can be taken from the mix ⁇ ture in a controlled fashion and so that the mixture "will have a more solid form at the region C.
  • the piston-cylinder devices acting on the matrix sec ⁇ tions 5a, 5b, 5c and 5d, of which the device 15 acting on the section 5a is shown, can be operated to deliver a short or a long working stroke, so as to move respec ⁇ tive matrix sections through a commensurate axial dis- tance with each stroke performed by respective piston- cylinder devices, while at the same time enabling a full working stroke to be completed at different selec ⁇ ted times.
  • the filler material in the plastic/filler mixture charged to the first feeder and precompressed in the vertical passage 2 may comprise heated sawdust, and the heat given off by the sawdust is transmitted directly to the plastics material pre- sent in the mixture.
  • This mixture is then fed by the horizontal screw-feeder comprising said conically tapering shaft and helix, the pitch of which decreases in a direction towards the centre of the matrix 5, therewith compressing the mixture to a greater degree of compression.
  • the space beneath the tubular passage 2 may be heated with the aid of heating coils, as can also the walls of the passage itself.
  • the matrix sections will preferably be held parallel, when the volume of the plastic material decreases at low temperature. It lies within the scope of the inven ⁇ tion, however, to position the matrix sections so that the elongated member produced will not press against said sections with an unnecessarily high force.
  • the plastics material present in the mixture is tacky and/or molten when the mixture is located within the regions B and C. Consequently, it is necessary to bring the mixture to a temperature at which this criterion is achieved.
  • this temperature is controlled and held constant, by controlling the speed of the screw-feeder.
  • the heat required can be obtained and controlled through the temperature of the starting material and/or by external heating.
  • Figure 3 is a side view of a compression section in the form of an extruder 30 in which there is mounted an internal screw-feeder 31 which carries a nozzle 32 on one end thereof.
  • the nozzle 32 is shown schematically and in side-view in Figure 1.
  • the nozzle 32 has a flange 33, which is attached to the extruder 30, and a narrowing part 34, and an outlet 35.
  • the outer parts 36, 37 of the outlet 35 are surrounded by the matrix-sections 5a and 5c, which are recipro- ⁇ fcatingly movable in the manner aforedescribed with reference to Figure 1.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Wood Science & Technology (AREA)
  • Forests & Forestry (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Adornments (AREA)

Abstract

The invention relates to a method and an apparatus for the continuous manufacture of an elongated member (10) from compressible material. A plastics material is delivered to a space (3) and there subjected to compression. The compressed material is pressed to a further space (7), defined by a matrix (5), where the material (10) is able to solidify. The matrix (5) has reciprocatingly movable walls. At least part of the thermal energy required to bring the plastics material to a tacky or molten state is generated by controlling the speed of a screw-feeder (4) forming part of the compression device.

Description

TITLE OF THE INVENTION: A method for manufacturing an elongated member and apparatus for carrying out the method
TECHNICAL FIELD
The present invention relates primarily to a method of manufacturing an elongated member, and in particular to a method in the continuous manufacture of an elon¬ gated member from a compressible and compressed start¬ ing material.
The invention also relates to apparatus for the con¬ tinuous manufacture of an elongated member with the use of compressible starting material.
The invention also relates to the use of a plastics material, particularly a plastics-material mixture as the compressible material.
BACKGROUND PRIOR ART
Various methods and apparatus are known for the manu- facture of elongated members or organs, these methods and apparatus being adapted to the material from which the elongated member is produced.
An example of the prior state of the art is found in International Patent Application No. PCT/SE84/00303, which teaches an apparatus for the manufacture of an elongated member in which a compression device located in a compression section is operative to displace and compact sequential, well-defined and binder-moistened material batches, and in which the compacted, indivi¬ dual batches are'passed sequentially through a high- frequency heating section.
A further example of the apparatus and methods known to the art is found in Swedish Patent Specification 415 547 (Swedish Patent Application 7809708-4), which teaches an apparatus in which the wall sections of the heating section are reciprocatingly movable in a hori- zontal direction and function, partially, as a means for transporting compacted material batches.
In each of the aforesaid cases, the elongated member is produced from separate, well-defined batches which are mutually separated by an interface or boundary region of mutually different degrees of compression and in which the fibre directions are also displaced relative to one another, to a certain extent, in the vertical plane. Hardening takes place in a heating section.
Swedish Patent Application 8804156-1 describes a method and apparatus for manufacturing an elongated member from a mixture of a plastics material and a filler, such as wood fibres, textile fibres and the like, by compacting the mixture when the plastics material is in a molten state.
SUMMARY OF THE INVENTION
TECHNICAL PROBLEMS
A study of the prior art within this technical field will reveal that a particularly challenging technical problem arises in the provision of a method and an apparatus by means of which an elongated member can be manufactured continuously in a simple and inexpensive manner, without the need of compacting separate batches of material, and where the elongated-member material is hot and comprises a compressible material, such as a 5 mixture of plastics material and filler, and which will enable the material to be cooled and therewith create conditions by means of which the temperature can be controlled readily in the compression section.
10 A particularly challenging technical problem also ari¬ ses in realizing those advantages which are afforded when the temperature of the mixture can be controlled at the compression-section inlet, optionally with the aid of externally applied heat, and when the thermal
15 energy generated by compression is utilized to soften and/or to melt the plastic content of the mixture, at least at the end of the compression section.
A particularly challenging technical problem also ari- 20 seε in realizing those advantages which are afforded when the heat generated in the compression section is controlled by controlling the speed of a screw-feeder located in the compression section, while taking into account prevailing production speeds. 25
A particularly challenging technical problem also ari¬ ses in realizing that the aforesaid technical problems can be solved when the plastic content of the starting mixture is precompacted in a molten or heated state, 3.0 and is then caused to solidify in a cooling section.
A particularly challenging technical problem also ari¬ ses in the provision of means whereby the degree of compression necessary for this purpose can be achieved with the aid of a simple screw-feeder provided with a helix of decreasing pitch, such that essentially the total necessary compression is effected in the screw- feeder itself.
A particularly challenging technical problem also ari¬ ses in the provision of a simple matrix-mould which will embrace the elongated member during its manufac¬ ture, and with which only limited measures need be taken for the purpose of reducing the friction between the matrix mould and the elongated member during its manufacture, by moving one or more walls of the matrix backwards and forwards, and by providing a matrix which is so configured that the resultant elongated member will have a circular or rectangular cross-section, or some other suitable cross-section.
A particularly challenging technical problem also ari¬ ses in the realization that the starting material may comprise waste material, where plastic material is of significance, and of realizing that the plastic mate¬ rial and filler should be mixed in appropriate propor¬ tions, particularly when the filler is a finely divided fibrous material r such as wood-fibre material, so as to obtain a mechanically strong elongated member.
A particularly challenging technical problem also ari¬ ses in the ability to realize the possibility that when the filler comprises a wood-fibre material, such as wood chips (sawdust , cutter chips) , and has been heat- dried in a preceding operation, the filler can be mixed with plastic material immediately after being dried, and the mixture further heated, when necessary, so as to convert the plastic content of the mixture to a tacky or liquid state, prior to compacting the mixture and subsequent cooling thereof to form said elongated member.
A particularly challenging technical problem will also be seen to exist in the provision of a reciprocatingly movable matrix-mould which is contained in a heating section at one end thereof and in a cooling section at the other end thereof, and to realize that the infeed device must accompany the matrix in one direction of movement thereof.
Finally, a particularly challenging technical problem also arises in realizing those advantages that are afforded by the use of an extruder which comprises a speed-controlled screw-press.
SOLUTION
With the intention of solving one or more of the afore- mentioned technical problems, the present invention relates primarily to a method of manufacturing conti¬ nuously an elongated member from compressible and com¬ pacted material.
The compressible material used comprises a mixture of plastics material and filler, and the mixture with its plastic content preferably in a molten state, is deli¬ vered to a first space and compacted therein. The com¬ pressed material is then pressed into another space, defined by a matrix mould, where the mixture is cooled so that the plastic content thereof will solidify.
In accordance with the present invention, the thermal energy generated during compression of the mixture is adapted so that the temperature of the plastic material will be sufficiently high to soften, preferably melt said material.
In accordance with one advantageous embodiment of the invention, the mixture is compressed with the aid of a screw-feeder, by controlling the speed of the screw- feeder and/or providing the helix of the screw-feeder with a pitch which decreases towards the aforesaid second space, so as to achieve desired compression within the screw-feeder.
According to a further embodiment of the invention the mixture can be precompressed with the aid of a further screw-feeder, but preferably at different rotational speeds. In this case, the further screw-feeder will preferably rotate at a higher speed than the first mentioned screw-feeder.
It is also proposed that the precompression screw-fee¬ der will be stationary in relation to one of the sec¬ tions of said matrix, namely one end-part of the upper matrix-section.
For the purpose of obtaining a flexurily rigid elon¬ gated member, it is proposed that the plastic content of the plastic-material/filler mixture comprises bet¬ ween 20 and 60%, say between 30-50%, normally about 40% of the total material content.
The filler used is preferably a newly dried and heated fibrous material, whereas the plastics material used may be waste-plastic, domestic plastic waste or some like inexpensive material. Means are preferably provided for cooling the part of the matrix located adjacent the extruder, preferably with the aid of water.
In accordance with one advantageous embodiment of the invention, the matrix is divided into sections, which are capable of being displaced synchronously or asynch¬ ronously in relation to one another, along the outer surfaces of the elongated member during the manufacture thereof.
The invention also relates to an apparatus for the continuous manufacture of an elongated member, this apparatus comprising a compression device having a rotatable shaft arranged concentrically with a matrix mould, and being operative to press the mixture through the matrix.
The apparatus also includes a preco pressing device which delivers precompressed mixture to the compressing device.
The matrix sections embrace the elongated member during its manufacture, and one or more of the matrix sections are reciprocatingly movable. The precompressing device coacts with one section.
Λ V NTAGES
Those advantages which may primarily be regarded as being characteristic of a method and apparatus accord¬ ing to the present invention are that possibilities are created in this way of enabling a mixture of filler and plastics material, with the plastics material prefer- ably in a liquid state and constituting a smaller pro¬ portion of the mixture than the filler, and in which the plastic material is optionally admixed with a rein¬ forcing material, such as a glass fibre material, to be pressed from a first heated space to an adjacent, col¬ der second space located downstream of the first men¬ tioned space, and to enable the elongated member to be manufactured with the aid of movable matrix sections from an inexpensive starting material and with low friction against the matrix walls, and therewith enabling the temperature of the plastics material to be controlled and maintained constant by the thermal energy generated by said compression.
This is achieved in the simplest manner by controlling the speed of a screw-feeder incorporated in the compre¬ ssion section in the form of an extruder.
The elongated member can be used as a nailing batten, in the manufacture of door and window frames or like structures, or can be cut into given, short lengths for use in the manufacture of loading pallets.
The primary characteristic features of a method for manufacturing an elongated member in accordance with the present invention are set forth in the characteriz¬ ing clause of the following Claim 1, whereas the pri¬ mary characteristic features of an apparatus for manu¬ facturing such a beam are set forth in the characteriz- ing clause of the following Claim 10.
BRIEF DESCRIPTION OF THE DRAWINGS
The invention will now be described in more detail with reference to two preferred embodiments of apparatus intended for the continuous manufacture of an elongated member from compressible and compressed material and with reference to the accompanying drawings, in which Figure 1 is a side view, partially in section, of a first apparatus constructed in accordance with the invention;
Figure 2 is a simplified sectional view taken on the line II-II i Figure 1; Figure 3 is a side view of a second embodiment of the inventive apparatus, which incorporates a compression section in the form of an extruder; and Figure 4 illustrates schematically a nozzle mounted on the extruder and capable of being connected to a matrix, not shown in detail.
DESCRIPTION OF PREFERRED EMBODIMENTS
The reference 1 in Figure 1 identifies a known appara¬ tus with which a plastics material can be mixed with a filler and/or a reinforcing material.
The apparatus shall be capable of enabling the plastics material to be heated and brought preferably to a mol¬ ten state, and in all events, to a tacky state.
When the filling material comprises cut or shredded paper and the plastics material with which it is to be admixed is heated either to a molten or a tacky state, it is preferred that the proportion of plastics mate¬ rial contained in the mixture will be less than 50% and preferably about 10%. The normal value in this respect will preferably lie between 20 and 50%, say about 40%.
When the plastic material is polyethylene, it may be present in a proportion of 25-40%. The apparatus 1 includes precompressing device in the form of a screw conveyor, by means of which a mixture A of plastics material and filler is fed to a first space 3, through a passage 2. The chamber 3 is conceived to be defined by the conically tapering shaft 4 and helix 8 of a further screw conveyor and also a tubular matrix 5 which embraces said conveyor. When leaving the pas¬ sage 2, the material A exhibits a degree of precompre- ssion which is commensurate with the pressure exerted on the mixture as it moves through the passage 2. The mixture A is then compressed successively to a much greater degree of compression by the screw-conveyor and tubular matrix 5, and at a region referenced B down¬ stream of the first space 3 the plastics material pre- sent in the mixture will be either in a molten or a tacky state.
As the mixture passes through the apparatus, in a direction to the right as seen in Figure 1, the plaε- tics material solidifies gradually and when the mixture has reached the position referenced C, it is assumed that the plastics material, and thus also the elongated member, will be essentially solid, and that in all events the plastic/filler mixture will have been com- pressed to its final degree of compression when it rea¬ ches the region of the apparatus referenced D, so as to form a finished elongated member or organ.
As shown in Figure 1, the precompressed plastic/filler mixture is moved by means of the screw-feeder 4,8 from the region B, where the plastic material begins to solidify, through the tubular matrix 5 and into the beginning of a third space 7. Compression of the mixture during its travel from region A to region B is effected with the aid of the screw-feeder 4, 8. he helix 8 of the screw-feeder has a pitch which decreases in a direction towards the third space 7, thereby providing the advantage that the mix¬ ture can be caused to have a predetermined degree of compression by the time it reaches the region B, due to t e successive decrease in the pitch of the helix 8.
The screw-feeder, comprising the conically tapering shaft 4 and helix 8, is rotated by means of drive means not shown.
For the purpose of reducing friction between the outer surfaces of the compressed mixture, or elongated mem¬ ber, shown at 10, and the inner surfaces of the tubular matrix 5, it is proposed that the matrix is divided into sections. Figure 2 is a cross-sectional view which illustrates a matrix of rectangular cross-section divi- ded into four sections 5a, 5b, 5c and 5d.
Each of these matrix sections is intended to coact with a hydraulic piston-cylinder device 15, the piston of which is reciprocatingly movable in the direction of the longitudinal axis of the elongated member 10. The different matrix sections can either be moved synchro¬ nously or asynchronously.
The matrix section 5a and 5c are held in position with the aid of rollers 16, 17, which extend along the whole length of the matrix 5 and which are present'in numbers that will ensure that the rollers fullfil the function satisfactorily. The matrix sections 5b and 5d are also held in position with the aid of -rollers, although not shown.
It is also proposed that cooling passages are provided in the matrix sections 5a, 5b, 5c and 5d in a manner known per se. so that heat can be taken from the mix¬ ture in a controlled fashion and so that the mixture "will have a more solid form at the region C.
The piston-cylinder devices acting on the matrix sec¬ tions 5a, 5b, 5c and 5d, of which the device 15 acting on the section 5a is shown, can be operated to deliver a short or a long working stroke, so as to move respec¬ tive matrix sections through a commensurate axial dis- tance with each stroke performed by respective piston- cylinder devices, while at the same time enabling a full working stroke to be completed at different selec¬ ted times.
Referring back to Figure 1, the filler material in the plastic/filler mixture charged to the first feeder and precompressed in the vertical passage 2 may comprise heated sawdust, and the heat given off by the sawdust is transmitted directly to the plastics material pre- sent in the mixture. This mixture is then fed by the horizontal screw-feeder comprising said conically tapering shaft and helix, the pitch of which decreases in a direction towards the centre of the matrix 5, therewith compressing the mixture to a greater degree of compression.
The space beneath the tubular passage 2 may be heated with the aid of heating coils, as can also the walls of the passage itself. The matrix sections will preferably be held parallel, when the volume of the plastic material decreases at low temperature. It lies within the scope of the inven¬ tion, however, to position the matrix sections so that the elongated member produced will not press against said sections with an unnecessarily high force.
ft is a significant feature of the present invention that the plastics material present in the mixture is tacky and/or molten when the mixture is located within the regions B and C. Consequently, it is necessary to bring the mixture to a temperature at which this criterion is achieved.
In accordance with the invention, this temperature is controlled and held constant, by controlling the speed of the screw-feeder.
High friction losses occur when this speed is exces- sively high, and low friction losses occur at exces¬ sively low speeds.
The heat required can be obtained and controlled through the temperature of the starting material and/or by external heating.
Figure 3 is a side view of a compression section in the form of an extruder 30 in which there is mounted an internal screw-feeder 31 which carries a nozzle 32 on one end thereof. The nozzle 32 is shown schematically and in side-view in Figure 1.
Since the construction of the extruder is known, it will not be described here in any detail.It should be noted, however, that the rotational speed of the screw- feeder 31 can be controlled.
The nozzle 32 has a flange 33, which is attached to the extruder 30, and a narrowing part 34, and an outlet 35. The outer parts 36, 37 of the outlet 35 are surrounded by the matrix-sections 5a and 5c, which are recipro- fcatingly movable in the manner aforedescribed with reference to Figure 1.
It will be understood that the invention is not restricted to the described and illustrated embodiments and that modifications can be made within the scope of the following claims.

Claims

1. A method of producing an elongated member from com¬ pressible and compressed material with the aid, in part of a plastics material which is delivered to a space and there subjected to compression and which is then pressed into a further space in which it is able to solidify, characterized in that the thermal energy generated by said compression, or compression, is adap- ted such as to bring the plastics material to a tem¬ perature which is sufficiently high to soften and/or melt the material.
2. A method according to Claim 1, characterized in that the thermal energy generated is controlled by control¬ ling the speed of a rotatable shaft.
3. A method according to Claim 1, characterized in that said compression is effected with the aid of a screw- feeder, the helix of which has a pitch which decreases in a direction towards a further space.
4. A method according to Claim 1, characterized by precompressing the material with the aid of a screw- feeder.
5. A method according to Claim 1, characterized by moving the material through a multi-section matrix; and by moving the matrix-sections backwards and forwards along the external surfaces of the elongated member under production.
6. A method according to Claim 3 or 4, characterized in that the precompression screw-feeder is fixed in rela- tion to one section of the matrix, the upper section.
7. A method according to Claim 1, 2, 3 or 4, charac¬ terized by mixing the plastics material with filler in proportions such that the plastics material will be present in a proportion of between 20 and 60%, prefer¬ ably about 40%.
8. A method according to Claim 1, characterized in that the plastics material used is waste-plastic, plastic domestic waste, or some like inexpensive plastic.
9. A method according to Claim 1 or 5, characterized by cooling the downstream part of the matrix, preferably with the aid of water.
10. Apparatus for manufacturing an elongated member, preferably in accordance with any one of the preceding claims, comprising a compressing device and a matrix which are arranged concentrically with one another and which are intended to compress a mixture of plastics material and a filler material, said compressing device functioning to press the mixture through the matrix; characterized in that the thermal energy generated by said compression can be adapted so that the mixture is brought to a temperature at which the plastic content thereof is softened and/or melted.
11. Apparatus according to Claim 10, characterized in that the thermal energy generated by said compression can be adapted such that the mixture is brought to a temperature at which the plastic content thereof will soften and/or melt.
12. Apparatus according to Claim 10, characterized in that the thermal energy generated is controlled by controlling the speed of a rotatable shaft.
13. Apparatus according to Claim 10, characterized in that compression is effected by the external supply of thermal energy.
14. Apparatus according to Claim 10, characterized in that compression is achieved with the aid of an extru¬ der comprising a controllable-speed screw-feeder.
15. Apparatus according to Claim 10, characterized by a multi-section matrix which embraces the elongated mem- ber during its manufacture, and in that one or more of said matrix sections is or are reciprocatingly movable.
16. Apparatus according to Claim 10, characterized in that the compressing device comprises a rotatable shaft which is rotated at a lower speed than the shaft of a precompressing device.
PCT/SE1989/000652 1988-11-17 1989-11-10 A method for manufacturing an elongated member and apparatus for carrying out the method WO1990005626A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
SE8804156A SE8804156L (en) 1988-11-17 1988-11-17 PREPARED TO MANUFACTURE A LONG-TREADED Beam AND APPARATUS FOR ITS PREPARATION
SE8804156-1 1988-11-17
SE8901782A SE8901782L (en) 1989-05-18 1989-05-18 Method and appts. for making elongated member - involves thermal energy generated by compression adapted to bring plastic material to temp. sufficiently high to soften material
SE8901782-6 1989-05-18

Publications (1)

Publication Number Publication Date
WO1990005626A1 true WO1990005626A1 (en) 1990-05-31

Family

ID=26660355

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SE1989/000652 WO1990005626A1 (en) 1988-11-17 1989-11-10 A method for manufacturing an elongated member and apparatus for carrying out the method

Country Status (2)

Country Link
AU (1) AU4508489A (en)
WO (1) WO1990005626A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1238792A2 (en) * 2001-01-13 2002-09-11 Karl Schedlbauer Method and apparatus for the continuous extrusion of solid or hollow profiles from small parts
EP1800831A3 (en) * 2005-12-23 2008-07-16 Imal S.R.L. Apparatus for extrusion pressing of loose wooden material and associated pressing method

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2304088A (en) * 1938-08-23 1942-12-08 Merrill G Hastings Apparatus for manufacturing filters
FR1589723A (en) * 1968-09-06 1970-04-06
DE1778230A1 (en) * 1968-04-09 1972-01-20 Actien Ges Der Gerresheimer Gl Process for the production of profiled bodies from polyethylene
DE2304088A1 (en) * 1972-01-28 1973-08-23 Mitsubishi Heavy Ind Ltd SCREW PRESS FOR EXTRUDING (EXTRUDING) NON-EXPANDABLE RESINS AND PROCEDURES FOR YOUR OPERATION
US4134714A (en) * 1977-04-18 1979-01-16 General Electric Company Multi-stage continuous plastic extrusion apparatus, and extrusion screw
SE410946B (en) * 1978-02-15 1979-11-19 Akerlund & Rausing Ab HALF PROFILE EXTRUDED FROM A BASIN OF POLYOLEFIN AND PAPER AND PROCEDURE
SE415547B (en) * 1978-09-15 1980-10-13 Andersson Kurt Goeran Device for manufacturing an elongate means
DE3412158A1 (en) * 1984-03-31 1985-10-03 Candid Neuenkirch Burkart Closed-loop control for an extruder system operating in a recycling process and extruder system
US4626398A (en) * 1984-04-19 1986-12-02 Roehm Gmbh Chemische Fabrik Process for the production of extruded web multiple panel with undulated webs

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2304088A (en) * 1938-08-23 1942-12-08 Merrill G Hastings Apparatus for manufacturing filters
DE1778230A1 (en) * 1968-04-09 1972-01-20 Actien Ges Der Gerresheimer Gl Process for the production of profiled bodies from polyethylene
FR1589723A (en) * 1968-09-06 1970-04-06
DE2304088A1 (en) * 1972-01-28 1973-08-23 Mitsubishi Heavy Ind Ltd SCREW PRESS FOR EXTRUDING (EXTRUDING) NON-EXPANDABLE RESINS AND PROCEDURES FOR YOUR OPERATION
US4134714A (en) * 1977-04-18 1979-01-16 General Electric Company Multi-stage continuous plastic extrusion apparatus, and extrusion screw
SE410946B (en) * 1978-02-15 1979-11-19 Akerlund & Rausing Ab HALF PROFILE EXTRUDED FROM A BASIN OF POLYOLEFIN AND PAPER AND PROCEDURE
SE415547B (en) * 1978-09-15 1980-10-13 Andersson Kurt Goeran Device for manufacturing an elongate means
DE3412158A1 (en) * 1984-03-31 1985-10-03 Candid Neuenkirch Burkart Closed-loop control for an extruder system operating in a recycling process and extruder system
US4626398A (en) * 1984-04-19 1986-12-02 Roehm Gmbh Chemische Fabrik Process for the production of extruded web multiple panel with undulated webs

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN, Vol. 11, No. 146, M587; & JP,A,61 279 524, publ. 1986-12-10, (JGC CORPORATION). *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1238792A2 (en) * 2001-01-13 2002-09-11 Karl Schedlbauer Method and apparatus for the continuous extrusion of solid or hollow profiles from small parts
EP1238792A3 (en) * 2001-01-13 2003-05-14 Karl Schedlbauer Method and apparatus for the continuous extrusion of solid or hollow profiles from small parts
EP1800831A3 (en) * 2005-12-23 2008-07-16 Imal S.R.L. Apparatus for extrusion pressing of loose wooden material and associated pressing method

Also Published As

Publication number Publication date
AU4508489A (en) 1990-06-12

Similar Documents

Publication Publication Date Title
EP0593444B1 (en) A method and arrangement for producing an elongated beam
US5094798A (en) Manufacture of lightweight structural profile
EP0278362B1 (en) Method and apparatus for the manufacture of thermoplastic preforms and preform
US4358418A (en) Method and apparatus for making compressed composite bodies of plant particles and binder
HU213041B (en) Method for manufacturing combined product comprising thermoplastic organic material and reinforcing fibres
US5352110A (en) Molding apparatus for molding fiber reinforced resin with plurality of roll pairs
WO1985003027A1 (en) Method of and apparatus for injection moulding of pvc products
EP1583647A1 (en) Method for producing composite materials such as thermoplastic resins with mineral and/or vegetable fillers
WO1990005626A1 (en) A method for manufacturing an elongated member and apparatus for carrying out the method
US5788901A (en) Method and apparatus for molding continuous lengths of plastic
EP3730275B1 (en) Method for the direct compounding of fibre-reinforced composite materials for the production of moulded plastic parts and direct compounding device
JP3608856B2 (en) Injection molding method and injection molding apparatus for long fiber reinforced thermoplastic resin
JPS5839063B2 (en) Extruder filling station closing device
CN212554964U (en) Extrusion mechanism for cable production plastic extruder
CN2420114Y (en) Board making device for Jinhe board
JPH0976328A (en) Method and apparatus for extrusion molding long fiber-reinforced thermoplastic resin
US3371378A (en) Apparatus for producing extruded tubes composed of extrudable thermosetting resins containing reinforcing fibers of fine texture
US20220152875A1 (en) Low pressure extruder, equipment and method for manufacturing a low-density plastic composite material, and the low-density plastic composite material
JP2923219B2 (en) Plasticization / injection method and screw pre-plasticization plasticization / injection device
CN219132979U (en) Ultrahigh molecular weight polyethylene heating mould pressing device for skis
CN220262069U (en) Composite material product with bar structure
EP0933185A2 (en) Method and apparatus for injection compression moulding of fibre reinforced plastics
CZ304467B6 (en) Process for extruding small vegetable parts mixed with binders and extruder for making the same
JPH054222A (en) Method and apparatus for manufacturing reinforcing material-containing panel
EP0020699B1 (en) Process and device for the manufacture of endless plastics products from thermo-hardenable mouldable material

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AT AU BB BG BR CH DE DK FI GB HU JP KP KR LK LU MC MG MW NL NO RO SD SE SU US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE BF BJ CF CG CH CM DE FR GA GB IT LU ML MR NL SE SN TD TG

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642