EP1563124A2 - Appareil et procede de formation de materiaux - Google Patents

Appareil et procede de formation de materiaux

Info

Publication number
EP1563124A2
EP1563124A2 EP03795823A EP03795823A EP1563124A2 EP 1563124 A2 EP1563124 A2 EP 1563124A2 EP 03795823 A EP03795823 A EP 03795823A EP 03795823 A EP03795823 A EP 03795823A EP 1563124 A2 EP1563124 A2 EP 1563124A2
Authority
EP
European Patent Office
Prior art keywords
tubular passage
extrusion apparatus
tubular
die
passage
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.)
Withdrawn
Application number
EP03795823A
Other languages
German (de)
English (en)
Inventor
David Philip Knight
Friedrich W. L. P. Upper Woods Farm VOLLRATH
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.)
Spin'tech Engineering GmbH
Spin Tech Engineering GmbH
Original Assignee
Spin'tech Engineering GmbH
Spin Tech Engineering GmbH
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 Spin'tech Engineering GmbH, Spin Tech Engineering GmbH filed Critical Spin'tech Engineering GmbH
Publication of EP1563124A2 publication Critical patent/EP1563124A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/28—Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30—Conjugate filaments; Spinnerette packs therefor
    • D01D5/34—Core-skin structure; Spinnerette packs therefor
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D4/00—Spinnerette packs; Cleaning thereof
    • D01D4/02—Spinnerettes
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/06—Wet spinning methods

Definitions

  • This invention relates to an apparatus and method for forming extruded material, such as filaments, fibres, ribbons, sheets or other solid products, from a liquid solution, such as a polymer solution (which term includes a protein solution or cellulose solution).
  • a liquid solution such as a polymer solution (which term includes a protein solution or cellulose solution).
  • Natural silks are fine, lustrous filaments produced by the silk-worm Bombyx mori and other invertebrate species. They offer advantages compared with the synthetic polymers currently used for the manufacture of materials.
  • the tensile strength and toughness of the dragline silks of certain spiders can exceed that of KevlerTM, the toughest and strongest man- made fibre.
  • Spider dragline silks also possess high thermal stability.
  • Many silks are also biodegradable and do not persist in the environment. They are recyclable and are produced by a highly efficient low pressure and low temperature process using only water as a solvent. The natural spinning process is remarkable in that an aqueous solution of protein is concerted into a tough and highly insoluble material.
  • Fibres produced by existing technological processes and apparatus suffer from the following disadvantages. Many show "die swell” which leads to some loss of molecular orientation with a consequent degradation of mechanical properties. Furthermore, existing processes are not energy efficient quiri g high temperatures and pressures to reduce the viscosity of the feedstock so that it can be forced trough a die. Separate stages are often required, for example for further "draw-down", to anneal the fibre with heat, and to process it through separate acid or alkaline treatment baths.
  • Patent Application EP-A-0 656 433 (Filtration Systems, Inc. and Japan Steel Works, Ltd.) which teaches a nozzle plate with a plurality of spinning holes. This document fails, however, to address the problem of die swell which occurs when the spun fibre or filament emerges from the exit of the nozzle plate.
  • extrusion apparatus with at least one tubular passage through which a core material is extrudable.
  • the core material forms the core of the fibre.
  • the core material is drawn down within the tubular passage at a distance of at least 0.5 mm from the outer exit opening of the tubular passage.
  • a fibre with an inner core and an outer coating there is a need to produce a fibre with an inner core and an outer coating.
  • This object of the invention is solved by providing a second tubular passage disposed about the first tubular passage. A coating material is extruded through the second tubular passage and is drawn down within the second tubular passage to form a coating about the core material. The coating can provide the fibre with further advantageous mechanical and other properties.
  • a component of the core material or the coating material in an initial zone of the first tubular passage or the second tubular passage forms rod-shape units that are substantially perpendicular to the internal surface of the first tubular passage and/or the second tubular passage.
  • a component of the core material in a subsequent zone of the first tubular passage or the second tubular passage has rod-shaped units which tumble within the first tubular passage and/or the second tubular passage.
  • the tumbling rod-shaped units aid in the drawn-down process.
  • the extrusion apparatus is provided with a ridged surface on an interior wall of the first tubular passage and/or the second tubular passage in order to further improve the drawdown process.
  • the height of the ridges on the ridged surface are preferably less than 10% than the diameter of first tubular passage and/or the second tubular passage. Best results are produced when the ridged surface coating has a surface energy lower than the surface energy of the core material.
  • the ridges on the ridged surface are substantially continuous and are substantially oriented parallel to the long axis of the tubular passages.
  • the ridges are preferably constructed from or coated with a hydrophobic material.
  • the objects of the invention are also solved by a method for fomiing spun material from a first solution comprising a first step of passing the first solution through one or more first tubular passages, and a second step of drawing the first solution down at a distance of at least 0.5 mm from an outer opening of the one or more first tubular passages to form a first spun material.
  • the method has a further step of passing a second solution through one or more second tubular passages disposed about the one or more first tubular passages and spinning the second solution about the first spun material to from the composite spun material.
  • a second solution is substantially fluid whilst the first spun material is substantially solid.
  • Figure 1 is a generalised schematic representation of apparatus for the formation of extruded materials form a spinning solution
  • Figure 2 is a schematic cross-sectional view along the longitudinal axis of a die assembly of the apparatus shown in Figure 1;
  • Figure 3 is a schematic perspective view of the die assembly shown in Figure 2;
  • Figure 4 is a schematic exploded view illustrating another embodiment of a die assembly of apparatus according to the invention.
  • Figure 5 is a view showing a number of die assemblies of Figure 4 assembled together in a unit to enable a plurality of fibres to be extruded.
  • Figure 6 is a view showing two die assemblies concentric to each other.
  • Figure 7 is a view illustrating tumbling of rod-shaped elements in the tubular passage.
  • Figure 8 is a cross-sectional view of the tubular passage.
  • each tubular passage suitably has an inlet at one end to receive the spinning solution and an outlet at the other for the formed or extruded material and is typically divided into three parts arranged consecutively, the first part or initial zone allowing for the pre-treatment and pre-orientation of the fibre-forming polymer molecules in the liquid feedstock prior to forming the material by draw down, the second region or subsequent zone in which draw down of theticianthread" takes place and which functions as a treatment and coating bath, and the third part or final part has an outlet or opening of restricted cross-section which serves to prevent the loss of the contents of theticiantreatment bath" with the emerging fibre and to provide for the commencement of an optional air drawing stage.
  • any solution or solvent or other phase or phases surrounding the fibre in the second part of the or each tubular passage also serves to lubricate the fibre as it moves through and out of the tubular passage.
  • each tubular passage typically has a convergent geometry typically with the diameter decreasing in a substantially hyperbolic fashion.
  • G. Y. Chen, J.A. Cuculo and P. A. Tucker in an article entitled “Characteristic and Design Procedure of Hyperbolic Dies” in the Journal of Polymer Sciences: Part B: Polymer Physics, Nol 30, 557-561 in 1992, it is reported that the orientation of molecules in a fibre can be improved by using a die with a convergent hyperbolic geometry instead of the more usual parallel capillary or conical dies.
  • the geometry of substantially all or part of the or each tubular passage may be varied to optimise the rate of elongational flow in the spinning solution (dope) and to vary the cross- sectional shape of the formed material produced from it.
  • the preferred substantially hyperbolic taper for part or all of the or each tubular passage maintains a slow and substantially constant elongational flow rate thus preventing unwanted disorientation of the fibre-forming molecules resulting from variation in the elongational flow rate or from premature formation of insoluble material before the dope has been appropriately reoriented.
  • a convergent taper to the tubular passage of the die will induce elongational flow which will tend to induce a substantially axial alignment in the fibre-forming molecules, short fibres or filler particles contained in the dope by exploiting the well known principle of elongational flow.
  • the principle of elongational flow through a divergent instead of the convergent die can be used to induce orientation in the hoop direction that is substantially transverse to the direction of flow through the divergent part of the die.
  • the diameter of the or each tubular passage may be varied to produce fibres of the desired diameter.
  • the rheology of the liquid feedstock in the tubular passage of the die is largely independent of scale, thus enabling the size of the apparatus to be scaled up or down.
  • the convergence of the tubular passage allows a wide range of drawing rates to be used typically ranging from 0.01 to 1000 mm sec "1 .
  • If fibres are being extruded they may typically have a diameter of from 0.1 to 100 ⁇ m.
  • the outlet of the tubular passage has a diameter of from 1 to 100 ⁇ m with the diameter of the inlet of the tubular passage being from 25 to 150 times greater depending on the extensional flow it is desired to produce.
  • Tubular passages of alternative cross-sectional shapes can be used to produce fibres, flat ribbons or sheets of extruded materials with other cross-sectional shapes.
  • All or part or parts of the walls of the or each tubular passage of the die assembly are constructed from or formed or moulded from selectively permeable and/or porous material, such as cellulose acetate-based membrane sheets.
  • the membrane can be substituted with diethylaminoethyl or carboxyl or carboxymethyl groups to help maintain protem-containing dopes in a state suitable for spinning.
  • the membrane can be rendered substantially hydrophobic with a siliconizing or silanizing solution or with polytetrafluoroethylene particles.
  • Other examples of permeable and/or porous material are hollow-fibre membranes, such as hollow fibres constructed from polysulfone, polyethyleneoxide-polysulfone blends, silicone or polyacrylonitrile.
  • the exclusion limit selected for the semipermeable membrane will depend on the size of the small molecular weight constituents of the dope but is typically less than 12 kDa.
  • All or part of the walls of the or each tubular passage can be constructed from selectively permeable and/or porous material in a number of different ways.
  • a selectively permeable and/or porous sheet can be held in place over a groove with suitable geometry cut into a piece of material to form the tubular passage.
  • two sheets of selectively permeable and/or porous material can be held in place on either side of a separator to construct the tubular passage.
  • a single sheet can be bent round to form a tubular passage.
  • a hollow tube of selectively permeable and/or porous material can also be used to construct all or part of the tubular passage.
  • a variety of methods are available to shape the tube into a die as is commonly known to a craftsman skilled in the art.
  • the interior walls may furthermore be substantially smooth or may be provided with "ridges" or bumps on at least part of the wall. The presence of such modifications in the walls aids in the draw-down process.
  • a control mechanism receiving inputs relating to the product being formed, for example the diameter of the extruded product and/or the resistance countered in the tubular passage, such as during extrusion through the outlet of the tubular passage, can be used to control, for example, polymer concentration, solute composition, ionic composition, pH, dielectric properties, osmotic potential and/or other physicochemical properties of the dope within the tubular passage.
  • the selective permeability and/or porosity of the walls of the or each tubular passage may also allow for the diffusion through the walls of further substances into the tubular passage(s) provided that these have a molecular weight lower than the exclusion limit of the selectively permeable material from which the walls of the tubular passage(s) are constructed.
  • the additional substances added to the dope in this manner may include surfactants; dopants; coating agents; cross-linking agents; hardeners; and plasticizers. Larger sized aggregates can be passed through the walls of the tubular passage if it is porous rather than being simply semipermeable.
  • the compartments surrounding the walls of the tubular passage or passages may act as one or more treatment zones or baths for conditioning the fibre as it passes through the tubular passage(s). Additional treatment baa occur after the material has exited the outlet of the tubular passage.
  • One or more regions of the or each tubular passage may be surrounded by one or more compartments arranged consecutively so as to act as a jacket or jackets to hold solution, solvent, gas or vapour in contact with the outer surface of the selectively permeable walls of the tubular passage(s).
  • solution, solvent, gar or vapour is circulated through the compartment or compartments.
  • the walls of the compartment or compartments are sealed to the outer surface of the wall or walls of the tubular passage(s) by methods that will be understood by a person skilled in the art.
  • the compartment or compartments serve to control the chemical and physical conditions within the or each tubular passage.
  • the compartments surrounding the tubular passage(s) serve to define the correct processing conditions within the dope at any point along the tubular passage(s).
  • parameters such as the temperature; hydrostatic pressure; concentration of fibre-forming material; pH; solute; ionic composition; dielectric constant; osmolarity or other physical or chemical parameter can be controlled in different regions of the tubular passage as the dope moves down the length of the die.
  • parameters such as the temperature; hydrostatic pressure; concentration of fibre-forming material; pH; solute; ionic composition; dielectric constant; osmolarity or other physical or chemical parameter can be controlled in different regions of the tubular passage as the dope moves down the length of the die.
  • a selectively permeable/porous membrane can be used to treat one side of a forming extrusion in a different way to the other side. This can be used, for example, to coat the extrusion or remove solvent from it asymmetrically in such a way that the extrusion can be made to curl or twist.
  • All or part of the draw down process may typically occur within the tubular passage of the die rather than at the outer face of the die assembly as occurs in existing spinning apparatus.
  • the former arrangement offers advantage over existing spinning apparatus.
  • the distortion of molecular alignment due to die swell is avoided.
  • the region of the die assembly after the internal commencement of the draw down taper can be used to apply coatings or treatments to the extrusion. Further, the last part of the die assembly is water lubricated by the solvent-rich phase surrounding the extrusion.
  • the apparatus can be used for forming fibres from dopes containing solutions of recombi ⁇ ant spider silk proteins or analogues or recombinant silk worm silk proteins or analogues or mixtures of such proteins or protein analogues or regenerated silk solution from silkworm silk.
  • dopes When these dopes are used it is necessary to store the dope at a pH above a critical value to prevent the premature formation of insoluble material. It will be appreciated that other constituents may be added to the dope to keep the proteins or protein analogues in solution.
  • constituents may then be removed through the semipermeable and/or porous walls when the dope has reached the appropriate portion of the tubular passage in which it is desired to induce the transition from liquid dope to solid product, e.g. thread or fibre.
  • the dope within the tubular passage can then be brought by dialysis against an appropriate acid or base or buffer solution to a pH value at or close to the critical value to induce aggregation or conformation change in one or more of the constituent proteins of the dope.
  • a pH change will promote the formation of an insoluble material.
  • a volatile base or acid or buffer can also be diflused through the walls of the or each tubular passage from a vapour phase in the surrounding compartment or jacket to adjust the pH of the dope to the desired value. Vapour phase treatment to adjust the pH can also occur after the extruded material has left the outlet of the die assembly.
  • the draw rate and length, wall thickness, geometry and material composition of the or each tubular passage may be varied along its length to provide different retention times and treatment conditions to optimise the process.
  • One or more regions of the walls defining the or each tubular passage can be made impermeable by coating their inner or outer surfaces with a suitable material to modify the internal environment in a length of the tubular passage using any coating method as will be understood by a person skilled in the art.
  • the inner surface of the walls of the or each tubular passage can be coated with suitable materials to reduce the friction between the walls of the tubular passage and the dope or fibre. Such a coating can also be used to induce appropriate interfacial molecular alignment at the walls of the tubular passage in liquid crystalline polymers when these are included in the dope.
  • a further embodiment allows for one or more additional components to be fed to the start of the or each tubular passage via concentric openings to allow two or more different dopes to be co-extruded through the same tubular passage allowing for the formation of one or more coats or layers to the fibre or fibres. This will be explained in more detail later by reference to Fig.6.
  • a further embodiment utilises a dope prepared from a phase separating rnixture containing two or more components which, for example, may be different proteins.
  • the removal or addition of components through the selectively permeable and/or porous material can be used to control the phase separation process to produce droplets of one or more components typically with a diameter of 100 to 1000 nm within the bulk phase in the final extrusion. These can be used to enhance the toughness and other mechanical properties of the extrusion.
  • the use of a convergent or divergent die conveniently induces elongational flow in the droplets to produce orientated and elongated filler particles or voids within the bulk phase.
  • a convergent die will orientate and elongate such droplets in a direction parallel to that of the formed product whereas a divergent die will tend to orientate the droplets in hoops transverse to the direction of flow of each particle within the tubular passage of the dope. Both types of arrangement can be used to enhance the properties of the formed product. Further it will be understood that the selectively permeable and/or porous walls of the or each tubular passage can be used to diffuse in or out chemicals to initiate the polymerisation of filler particles.
  • the spinning apparatus with one or more tubular passages surrounded by a compartment or compartments to act as jackets can be' constructed by one or two stage moulding or other methods known to a person skilled in the art. It will be appreciated that a moulding process can be used to create simple or complex profiles for the or each tubular passage and the outlet of the die assembly. Very small flexible lips can be formed, e.g. moulded, at the outlet to prevent the escape of the contents of the treatment bath and act as a restriction to enable an optional additional air drawing stage or wet drawing after the material has left the outlet of the die assembly should this be required.
  • the microscopic profile of the inner surface of the lips at the outlet can be used to modify the texture of the surface coating of the extruded material.
  • the jackets and supports for the tubular passages can be constructed from two or more components formed by injection moulding or constructed in other ways as will be understood by a person skilled in the arts. It will be appreciated that this method of construction is modular and that a number of such modules can be assembled in parallel to produce simultaneously a number of fibres or other shaped products. Sheet materials can be produced by a row or rows of such modules.
  • Such a modular arrangement allows for the use of manifolds to supply dope to the inlet of the tubular passage(s) and to supply and remove processing solvents, solutions, gases or vapours to and from the jacket or jackets surrounding the tubular passages. Additional components may be added if desired. Potential modifications to the arrangements shown will be apparent to persons skilled in the art.
  • the or each tubular passage may be made self-starting and self-cleaning. It will be appreciated that blockage of spinning dies during the commercial production of extruded materials is time-consuming and costly.
  • the walls of the tubular passage may be constructed by two or more jackets arranged in sequence. The pressure in each of these jackets can be varied independently by methods that will be understood by a craftsman skilled in the art. Pressure changes in the jackets can be used to change the diameter of different regions of the tubular passage in a manner analogous to a peristaltic pump to pump the dope to the outlet to commence the drawing of fibres or to clear a blockage.
  • the pressure in the sealed compartments surrounding the tubular passage(s) may be controlled to define and modify the geometry of the tubular passage to optimise spinning conditions.
  • the semipermeable or porous membrane can be used to introduce agents to help clean blocked dies.
  • agents include ammonia vapour or solutions, including dilute solutions, of alkalis or alkaline buffers.
  • filler particles or short fibres included in the dope may be orientated as they flow through the tubular passage by exploiting the well understood principle of elongational flow. It will be understood that the substantially axial orientation of such filler particles or short fibres will be produced by a convergent tubular passage while a divergent one will produce orientation in the hoop direction that is approximately transverse to the log axis of the extruded material. Both patterns of orientation confer additional useful properties on the fibre.
  • a convergent or divergent geometry of all or part of the or each tubular passage will also serve to elongate and orientate small fluid droplets of an additional solvent or solution or other phase or phases or additional unpolymerised polymer or polymers present in the dope as supplied to the tubular passage or arising by a process of phase separation within the dope.
  • the presence of elongated and well orientated narrow inclusions formed by either a convergent or divergent tubular passage can be used to confer additional useful properties to the extruded material.
  • the apparatus my be arranged in such a way that two or more fibres are formed in parallel and twisted around each other or crimped or wound onto a former or coated or left uncoated as desired.
  • the fibres can be drawn through a coating bath and subsequently through a convergent die to give rise to a "sea and island" composite material as will be understood by a person skilled in the art.
  • One or more rows of dies or one or more dies with slit or annular opening can be used to form sheet materials.
  • FIG. 1 shows a schematic apparatus for the formation of extruded materials from a extrusion solution such as lyotropic liquid crystalline polymer or other polymers or polymer mixtures.
  • the apparatus comprises a dope reservoir 1 containing dope 25; a pressure regulating valve or pump means 2 which maintains a constant output pressure under normal operating conditions; a connecting pipe 3; and a spinning die assembly 4 comprising at least one spinning tube or die further described in figures 2 to 5.
  • a take-up drum 5 of any known construction draws out and reels up extruded material at a constant tension exiting from the outlet of the die assembly 3.
  • the pressure regulating valve or pump means 2 may be any device normally producing a constant pressure commonly known to a person skilled in the art.
  • dope 25 is passed from the feedstock reservoir 1 at a constant low pressure by means of the regulating valve or pump means 2 via the connecting pipe 3 to the inlet of the spinning die assembly 4.
  • the die assembly 4 is shown in greater detail in Figures 2 and 3 and comprises a first spinning tube or die 8 upstream of a second spinning tube or die 12, the dies together defining a tubular passage 17 for spinning solution 25 through thee die assembly 4.
  • the die 12 has an interior wall 18 and is divided into an initial zone 60 and a subsequent zone 62.
  • the dies 8 and 12 are made of semipermeable and/or porous material, such as cellulose acetate membranes or sheets. Other examples of suitable semipermeable and/or porous materials are diethylanjunoethyl or carboxyl or carboxymethyl groups which help to maintain protein- containing dopes in a state suitable for spinning.
  • Hollow-fibre membranes material such hollow-fibre membranes being made from polysulfone, polythyleneoyide-polysulfone blends, silicone or polyacrylonitrile can also be used.
  • the exclusion limit selected for the semipermeable membrane will depend on the size of the small molecular weight constituents of the spinning dope 25 but is typically less than 12 kDa.
  • the die 8 is held at its upstream end by a tapered adaptor 6 positioned at the inlet end of the die assembly 4 and at its downstream end by a tapered adaptor 7 positioned internally in the die assembly 4.
  • the die 8 is held at its upstream end by the adaptor 7 and at its downstream end by a spigot 13 at the outlet of the die assembly 4.
  • the die 8 has a convergent, preferably hyperbolic, internal passage and the geometrical taper is preferably continued with the internal passage of the die 12. This can be achieved during construction by softening a semipermeable tube or die an a warmed suitably tapered mandrel, or by other methods as will be appreciated by a craftsman skilled in the art before fitting the spinning tube or die into the apparatus.
  • the internal passages of the dies 8 and 12 together provide the tubular passage 17 for spinning solution from the inlet to the outlet of the die assembly 4.
  • a jacket 9 surrounds the die 8 and may contain a fluid, e.g. a solvent, solution, gas or vapour to control the processing conditions within the spinning tube or die 8.
  • the jacket 9 is fitted with an inlet 10 and an outlet 11 to control flow of fluid into and out of the jacket.
  • a further jacket 14 surrounds the tube or die 12 and is fitted with a fluid inlet 15 and a fluid outlet 16 to enable fluid, e.g. solvent, solution or gas, to be passed into and out of the jacket 14 in contact with the semipermeable/porous walls of the die 12.
  • a die 8 may be constructed from material which is not semipermeable or porous but which is preferably tapered, e.g. convergentiy, and may be temperature-controlled by circulation fluid at a predetermined temperature through the jacket 9.
  • spinning solution or dope 25 e.g. a polymer solution
  • the fluid passing through the jacket 9 may merely serve to heat or maintain the dope 25 at the correct temperature or provide the correct external pressure to the walls of the die 8. in this case it is not essential for the walls of the die to be made of semipermeable and/or material.
  • the temperature of the dies 8 and 12 for the extrusion of protem-containing dopes 25 should typically be maintained at a temperature of about 20°C but spinning may be carried out at temperatures as low as 2°C and as high as 40°C.
  • the temperature of the dies 8 and 12 for the extrusion of dopes can more generally be as high as 100°C providing that the material is not destroyed at this temperature.
  • the pressure of the fluid, liquid or gas, in the jackets surrounding the walls of the tubular passage 17 is typically maintained at a pressure close to that at which the dope 25 is supplied to the die assembly 4. However the pressure can be somewhat higher or lower depending on the geometry of the dies and the strength of the generally flexible semipermeable and/or porous membrane. "Chemical" treatment of the dope 25 occurs during “draw down” as the dope 25 passes through the die 12 although chemical treatment may also occur as the dope 25 passes through the die 8 if the walls of the latter are at least partly made of semipermeable material.
  • the abrupt pulling away of the dope 25 from the walls of the die 12 at 12A indicates the internal draw down of the "fibre". This occurs at the boundary of the initial zone 60 and the subsequent zone 62.
  • the pulling away of the "fibre" from the die walls at 12A occurs at a place in the tubular die 12 where the force required to produce extensional flow to create a new surface just falls below the force required to flow the dope through the die 12 in contact with the die walls. This is the position at which the surface energy of the interior wall 18 becomes lower than the surface energy of the dope 25.
  • the position of 12A will depend on: the changing rheological properties of the dope; the rate and force of drawing; the surface properties of the die 12; the surface properties of the lining of the die 12; and the properties of the dope and the aqueous phase surrounding the dope.
  • the position of 12A should be at least 0.5 mm from the outer opening or spigot 13.
  • a surface 66 of the interior wall 18 of the die 12 is provided with ridges 68 to facilitate the draw down of the fibre at position 12A.
  • ridges 68 have a height of typically less than 10% of the diameter of the die 12.
  • the diameter of the die 12 at this position is 20 ⁇ m and the ridges 68 are 0.5 ⁇ m high.
  • the ridges 68 could be between 100 nm and 20 ⁇ m high. It is believed that draw-down of the fibre occurs because in the die 8 and the initial zone 60 of the die 12, rod-shaped units 64 in the dope 25 are arranged substantially perpendicular to the interior wall 18. At position 12A, these rod-shaped units start to "tumble" within the dope 25 and thus increase the viscosity and decrease the surface energy of the dope 25. This tumbling is aided by the presence of the ridges 68 on the interior wall 18.
  • the temperature, pH, osmotic potential, colloid osmotic potential, solute composition, ionic composition, hydrostatic pressure or other physical or chemical factors of the solution, solvent gas or vapour supplied to the jacket(s) control or regulate the conditions inside the tubular passage 17 as is commonly understood by a craftsman skilled in the art.
  • Chemicals in the fluid supplied to the jacket(s) 9 are able to pass through the semipermeable and /or porous walls of the tubular passage 17 to "treat" the dope 25 passing therethrough. It is als ⁇ possible for chemicals in the dope 25 to pass outwardly through the semipermeable and/or porous walls of the tubular passage 17.
  • the fluids supplied to the dope 17 will obviously depend on the type of dope 25 used and the semipermeable and/or porous membranes used.
  • the jacket 9 may contain 100 mM Tris or PPES buffer solution, typically at a pH of 7.4, and 400 mM sodium chloride to help maintain the folded state of the protein.
  • the jacket 14 may contain 100 mM ammonium acetate buffer solution at al lower pH, typically ⁇ 5.0, and 250 mM potassium chloride to encourage the unfolding /refolding of the protein.
  • High molecular weight polyethylene glycol can be added to the solution in both jackets to maintain or reduce the concentration of water in the dope 25.
  • the spinning tube or die 12 can be hanked or coiled or arranged in other ways between the tapered collar 7 and the spigot 13.
  • the diameter and cross-sectional shape or the exit 13 can be varied or adjusted to suit the diameter and cross sectional shape of the formed material.
  • the typical diameter of the outlet is from 1 to 100 ⁇ m and the typical diameter of the inlet to the tubular passage 17 would be from 25 to 150 times greater than the outlet diameter depending on the extent of the extensional flow.
  • the arrangements and proportions shown in Figure 2 are purely exemplary and thus that additionally components may be added if desired. Potential modifications to the arrangements shown in Figure 2 will be apparent to persons skilled in the art.
  • Figure 4 shows a module containing three spinning tubes or dies 12 mounted within a housing defining three "jackets" 14, the same numbering being used as in the previous embodiments to identify the same or similar parts.
  • the arrangements and proportions shown in Figure 2 are purely exemplary and thus additional components may be added if desired. Potential modifications to the arrangements shown in Figure 4 will be apparent to persons skilled in the art, including the provision of fewer or more dies 12 or jackets 14.
  • Figure 5 shows how two or more modular units constructed from the apparatus shown in Figure 4 can be held together to enable a plurality of extruded fibres to be produced. It will be appreciated that the arrangements and proportions shown in Figure 5 are purely exemplary and thus additional components may be added if desired. Potential modifications to the arrangements shown in Figure 5 will be apparent to persons skilled in the art.
  • the permeability or porosity of the walls of the tubular passage may be the same throughout the length of the latter. Alternatively, however, if the tubular passage 17 passes through more than one treatment zone the permeability/porosity of the walls of the tubular passage may change from treatment zone to treatment zone by using different semipermeable or porous materials for the walls of the tubular passage.
  • the walls of the tubular passage 17 may comprise: semipermeable material of the same permeability throughout the length of the tubular passage; semipermeable material of different permeability for different portions of the tubular passage; porous material of the same porosity throughout the length of the tubular passage 17; porous material of different porosity for different portions of the passage; or semipermeable material for one or more portions of the length of the tubular passage and porous material for one or more other portions of the tubular passage. As mentioned above, some portions of the walls of the tubular passage may be non-permeable.
  • suitable semipermeable materials are: cellulose derivatives, expanded PTFE, polysulfone, polyethylenoxide-polysulfbne blends, and silicone polyacrylonitrile blends.
  • suitable porous materials are: polyacrylate, poly (lactide-co- glycolide), porous PTFE, porous silicon, porous polyethylene, cellulose derivatives and chitosan.
  • Figure 6 shows a further embodiment of the invention in which a coating dope or material 27 is in a second tubular passage 50.
  • the second tubular passage 50 is substantially concentric wrffi the first tubular passage 17.
  • the first tubular passage 17 has an inner opening 54 disposed within the second tubular passage 50.
  • the dope 25 forms a core material for a fibre or filament.
  • the core is produced in accordance with the techniques described above.
  • the coating material 27 of the fibre is draw-down at a position 52 over the core of the fibre to form composite spun material 31. Construction of the second tubular passage 50 is similar to that of the first tubular passage 17.
  • the apparatus is suitable for the information of fibres of sheets from all solutions of lyotropic liquid crystal polymers whether synthetic or man-made or natural or modified or copolymer mixtures or solutions of recombinant proteins or analogues derived from them or mixtures of these.
  • these include collagens; certain cellulose derivatives; spidroins; fibroins; recombinant protein analogues based on spidroins, or fibroins, and poly (p-phenylene terephthalaes).
  • the method is also suitable for use with other polymers or polymer mixtures provided that they are dissolved in solvents, whether aqueous or non-aqueous, protein solutions, cellulose or chitin solutions.
  • the use of one or more semipermeable and/or porous treatment zones can be used for dies or die assemblies having essentially annular or elongated slit openings used for the formation of sheet materials.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Textile Engineering (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Artificial Filaments (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

L'invention a trait à un appareil d'extrusion et à un procédé d'extrusion de fibres. Ledit appareil d'extrusion possède un premier passage tubulaire (17), à travers lequel un matériau noyau (25) peut être extrudé. Ledit passage tubulaire (17) comporte une première ouverture de sortie (13). En cours de fonctionnement, le matériau noyau (25) est étiré à l'intérieur du premier passage tubulaire (17), à une première distance, d'au moins 0,5 mm, de l'ouverture de sortie extérieure (13). Dans un autre mode de réalisation, l'appareil d'extrusion comprend un second passage tubulaire (50), à travers lequel un matériau de revêtement (27) peut être extrudé. Le second passage tubulaire est disposé à proximité du premier passage tubulaire (17), et comporte une ouverture intérieure (52). Ladite ouverture intérieure (52) est située à l'intérieur du second passage tubulaire (50) et, en cours de fonctionnement, le matériau de revêtement (27) est étiré à l'intérieur du second passage tubulaire (50).
EP03795823A 2002-11-14 2003-11-14 Appareil et procede de formation de materiaux Withdrawn EP1563124A2 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB0226574A GB0226574D0 (en) 2002-11-14 2002-11-14 Apparatus and method for forming materials
GB0226574 2002-11-14
PCT/EP2003/012848 WO2004044279A2 (fr) 2002-11-14 2003-11-14 Appareil et procede de formation de materiaux

Publications (1)

Publication Number Publication Date
EP1563124A2 true EP1563124A2 (fr) 2005-08-17

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EP03795823A Withdrawn EP1563124A2 (fr) 2002-11-14 2003-11-14 Appareil et procede de formation de materiaux

Country Status (7)

Country Link
EP (1) EP1563124A2 (fr)
AU (1) AU2003298118A1 (fr)
CA (1) CA2505864A1 (fr)
GB (1) GB0226574D0 (fr)
RU (1) RU2005118751A (fr)
TR (1) TR200502685T1 (fr)
WO (1) WO2004044279A2 (fr)

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2450457A (en) * 1945-11-09 1948-10-05 Gen Tire & Rubber Co Process and apparatus for coagulating a coagulable fluid
GB1083008A (en) * 1963-12-07 1967-09-13 Kanegafuchi Spinning Co Ltd Improvements in or relating to composite filaments
JP2668849B2 (ja) * 1993-12-02 1997-10-27 惠一 村上 紡糸用口金の製造方法
US5556589A (en) * 1994-09-07 1996-09-17 Hercules Incorporated Process of using a spin pack for multicomponent fibers
ID17252A (id) * 1996-04-29 1997-12-11 Akzo Nobel Nv Proses pembuatan obyek yang terbuat dari selulosa
EP0997560A4 (fr) * 1998-04-07 2004-10-13 Toray Industries Ensemble filiere de filage par fusion et procede de fabrication de fibres synthetiques
GB9927950D0 (en) * 1999-11-27 2000-01-26 Knight David P Apparatus and method for forming materials

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2004044279A3 *

Also Published As

Publication number Publication date
RU2005118751A (ru) 2006-01-20
TR200502685T1 (tr) 2005-12-21
WO2004044279A2 (fr) 2004-05-27
CA2505864A1 (fr) 2004-05-27
GB0226574D0 (en) 2002-12-18
AU2003298118A1 (en) 2004-06-03
WO2004044279A3 (fr) 2004-07-29

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