fig1 shows conventional melt extrusion apparatus used in performing the process of the invention , by way of example . the apparatus has a powder hopper 1 leading to a barrel 2 containing an archimedean feed screw 3 . the extruder barrel 2 has three zones feed , compression and metering zones 4 , 5 , 6 . the screw 3 has a 3 : 1 compression ratio , a 1 inch ( 2 . 54 cm ) diameter and a length - to - diameter ratio of 24 : 1 . the barrel 2 is connected via a diameter - reducing adapter section 7 to a die 8 comprising a 40 - hole spinneret , the holes being of 0 . 55 mm diameter . in front of the die there is a cooling roller 9 with a pinch roller 10 and an air knife 11 , and subsequent guide rollers 12 - 14 , a guide rail 15 and a wind - up roller 16 . a heater is provided ( not shown ) for heating the barrel 2 at the three separate zones 4 , 5 , 6 along its length , and also at adapter 7 and die 8 . the heating arrangement permits different temperatures to be maintained for each of these and conventionally this would be in an increasing manner from zone one 4 to zone three 6 . in use , for polypropylene powder , zone temperature differences might typically be from 10 - 20 ° c . in accordance with an example of the present invention a temperature of 159 ° c . is maintained throughout the three zones 4 - 6 of the barrel 2 , adapter 7 , and die 8 , and polypropylene powder is fed from the hopper 1 to the barrel 2 . the polypropylene powder in this example has a particle diameter & lt ; 300 μm , the diameters of individual particles varying within a range of ± 10 % of a medium diameter . all particles have irregular shapes and rough surfaces . the polymer used is coathylene pb 0580 , as produced by plast - labor s . a ., ch - 1630 bulle , switzerland . the screw 3 is driven at a controlled relatively slow rate of 10 rpm ( corresponding to a throughput of 3 . 6 gms per minute ) and this causes the powder to be advanced along the zones 4 - 6 of the barrel 2 to the adapter 7 and the die 8 . this speed , is selected in relation to other parameters , namely the powder morphology , the temperature , the length of the barrel 2 and adapter 7 , and the cross - sectional characteristics of the barrel 2 , adapter 7 and holes of the die 8 . the powder particles are thereby caused to cohere together and flow through the die holes . the screw speed is selected to be as slow as possible , and the temperature is as low as possible , whilst achieving smooth fibre characteristics . the temperature is below the melting point of the polymer so that the particles cohere to form a continuous , fluent body without losing their integrity . thus , although the apparatus is derived from conventional melt extrusion apparatus , the process involves ‘ melt ’ or flow spinning , but without melt extrusion occurring . in particular , and as discussed further below , the powder particles are sintered together at a temperature low enough to allow some degree of surface melting but not high enough to give bulk melting . the material flows through the die 8 and is taken up by the pinch rollers 9 , 10 without application of any appreciable traction . the material is therefore spun or extruded but not significantly drawn . the ‘ molten ’ filaments leaving the die 8 are picked up with a metal rod and draped around the cooling roller 9 prior to engagement of the pinch roller 10 . the pinch roller 10 is then engaged and the air knife moved in position at a setting of 5 mm above the path of the filaments . from the pinch rollers 9 , 10 , the filaments are taken down from the cooling roller 10 and are passed under roller 12 , up and over roller 13 and then straight across to roller 14 . the filaments are then fed vertically downwards and slid over the guide rail 15 to the wind - up roller 16 . in this example the rollers 9 , 10 , 12 - 14 , 16 are driven to run at a slow speed of 2 meters per minute to achieve guide of the filaments without applying any appreciable drawing or traction forces . however , at higher barrel extrusion speeds , proportionally higher roller speeds would enable the same fibre characteristics to be achieved . other rollers such as would be used with apparatus of this kind where drawing is required are not used here . as a consequence of the above described procedure the filamentary material produced from the die 5 has a micro - structure of fibrils 17 linked by nodes 18 , as shown in fig2 , which gives rise to auxetic properties . this microstructure is known to provide auxetic properties but has hitherto been obtained by compaction and sintering of the polymer powder , which may be followed by draw extrusion of a relatively large diameter cylindrical rod ( say up to 10 or 15 mm ). it has been found , surprisingly , that the auxetic microstructure can be obtained with the above described ‘ melt ’ spinning process without use of separate compacting and sintering stages or paying careful attention to die geometry . the following table , table 1 , gives detailed parameters for the above described example of the invention , in the column identified batch m . these parameters are compared with parameters of two other batches , batch b and batch h using the same polypropylene powder . also , characteristic parameters of a sample of raw powder are shown . as can be seen from the table , the batch of raw powder examined starts to melt at 149 ° c . and melts completely at 165 ° c ., and the % crystallinity of the powder is 47 . 8 %. parameters were derived using differential scanning calorimetry conducted on a polymer labs pl dsc under flowing nitrogen at a heating rate of 10 ° c ./ min from 30 - 200 ° c . batch m has somewhat similar characteristic parameters to the raw powder , particularly the crystallinity percentage . micrographic analysis of batch m fibres showed that they had auxetic properties . that is , the fibres showed a structure of fibrils attached to modules . also , extension of the fibres caused these to expand laterally . batch b and batch h were processed at higher temperatures and higher throughputs . as shown in the table this resulted in a much reduced crystallinity percentage . micrographic analysis did not reveal any significant auxetic properties . this demonstrates that , to attain auxetic properties , it is desirable for the powder particles to be sintered together at a temperature low enough to allow some degree of surface melting yet not high enough to enable bulk melting whereby the fibres remain as close as possible to the raw powder particularly with regard to the dsc - derived % crystallinity . the resulting filamentary auxetic material can be used as reinforcing fibres , or in textile structures , and has advantageous properties suited to a range of applications . auxetic fibres can be used as fibre reinforcements in composite materials e . g . polyolefin auxetic fibres in a polyolefin matrix . the auxetic fibres improve resistance to fibre pull out and fibre fracture toughness , and give enhanced energy absorption properties . sonic , ultrasonic and impact energy can be absorbed enabling superior composites to be made for sound insulation of walls of buildings , body parts for submarines or other vehicles , etc , bumpers for cars , etc . auxetic materials also respond to impact to give local densification thereby giving enhanced indentation resilience . auxetic fibres can be used alone or in combination with other materials for personal protective clothing or equipment as a consequence of the superior energy absorption and impact resistance properties . crash helmets and body armour ( e . g . bullet proof vests ) are examples of applications . for such an application it may be desirable to make the protective material in the form of an auxetic macrostructure made from auxetic fibres ( i . e . a hierarchical auxetic material ). this would enable a single - component protective material to perform the combined energy absorption and indentation resistance roles , rather than having separate layers to perform each of these tasks in a dual - component material . these properties should also lead to enhanced sports protective clothing , e . g . shin pads , knee pads , batting gloves etc . the possibility exists of producing protective clothing made from auxetic fibres which have equivalent protective performance to those made from non - auxetic fibres but which are lighter and / or thinner due to the benefits associated with the auxetic property . auxetic materials have pore size / shape and permeability variations leading to superior filtration / separation performance in several ways when compared to non - auxetic materials . application of an applied tensile load on a non - auxetic porous material causes the pores to elongate in the direction of the applied load , which would tend to increase the filter porosity . however , the positive poisson &# 39 ; s ratio of non - auxetic materials causes the pores to contract in the transverse direction , thus reducing the overall porosity in competition with the increase in porosity due to longitudinal pore extension . for an auxetic porous material , on the other hand , the pores extend in both the loading and transverse directions , leading to enhanced porosity variations when compared with the non - auxetic equivalent . benefits for auxetic filter materials , therefore , include release of entrapped particulates ( leading to potential for cleanable filters and filters / membranes where a controlled release of a dose of particles / cells / molecules of a specific size / shape are required , e . g . drug - release materials ) and self - regulating filters to compensate for pressure build - up due to filter fouling . non - auxetic microporous polypropylene fibres have been proposed for use in cloth filters . also , non - auxetic microporous fibres , possibly hollow , are themselves used as separation materials in which a two - phase mixture ( solid and liquid , for example ) is passed down the middle of the fibre , with one phase then passing through the walls of the fibre whilst the other continues to pass down the middle . hollow polypropylene fibres are employed in , for example , mechanical lung applications in which carbon dioxide is removed from the blood of the patient , and fresh oxygen is supplied to the patient . an auxetic equivalent should have superior performance in terms of selectivity and cleanability in these applications . polypropylene fibres are employed in rope or cord and fishnet applications due to their high strength and low weight ( i . e . floatation ) properties . in addition to the usual methods of strengthening ropes ( due to twisting mechanisms between fibres etc ) the auxetic effect can further enhance the strength properties of ropes and fishnets . in the case of two adjacent non - auxetic fibres , application of tension of the fibres causes them to elongate in the direction of tension and to contract radially due to the positive poisson &# 39 ; s ratio . hence ( neglecting twist and friction effects etc .) extension of the fibres is simply governed by the fibre young &# 39 ; s modulus . for two adjacent auxetic fibres , however , the elongation in the direction of applied tension is accompanied by a concomitant increase in radial expansion due to the negative poisson &# 39 ; s ratio . for two fibres in contact this causes radial compression between the fibres which is , therefore , converted into a longitudinal contraction ( due to the negative poisson &# 39 ; s ratio ) in direct competition to the extension due to the applied tensile load . hence , in this case the overall longitudinal extension of the fibres is lower than that which would be expected from the fibre young &# 39 ; s modulus as a direct consequence of the auxetic effect . in other words , to a first approximation the extension of two or more non - auxetic fibres in radial contact will be equal to that of a single fibre of equal young &# 39 ; s modulus in isolation and subject to the same applied stress , whereas the extension of two or more auxetic fibres in radial contact will be less than - that of a single fibre of equal young &# 39 ; s modulus in isolation . hence , a rope or fishnet made from auxetic fibres will have enhanced strength properties . in addition to the strength enhancements , auxetic fibres also exhibit improved wear resistance due to having enhanced indentation properties . this leads to ropes and fishnets having enhanced abrasion properties to counteract the effects of ingress of , for example , sand grains during use . improved wear resistance should also be useful in other fibre applications such as upholstery fabrics etc . naturally - occurring auxetic biomaterials are known , for example cow teat skin , cat skin and certain forms of bone . in developing synthetic replacement biomaterials it is desirable to consider auxetic functionality in order to ensure an adequate match in the mechanical properties of the real and synthetic materials . currently , fibrous biomedical materials include cartilage , surgical implants and suture anchors or muscle / ligament anchors , where the additional benefit of a microporous structure should promote bone in - growth . the use of auxetic fibres leads to benefits by ensuring an adequate match in mechanical properties , improved strength and wear resistance for load bearing components ( e . g . cartilage ), and improved ‘ anchoring ’ properties . auxetic fibres can be used in bandages and pressure pads in wound care . important properties in these applications may include that the bandage maintains pressure on the wound to prevent swelling of the wound , and enables the wound to breathe through the macropores of the bandage structure whilst also preventing infection of the wound . ideally the bandage may also enable wound - healing to occur by application of an appropriate wound - healing agent . a tubular bandage or pad or strip formed from auxetic fibres can be applied around a limb . auxetic fibres would tend to act to maintain the breathability and pressure applied by an auxetic bandage on the wound despite any swelling of the wound . furthermore , if the auxetic fibres are ‘ loaded ’ with a wound - healing component ( i . e . the wound - healing component particles are initially entrapped within the auxetic fibre microstructure ) then the extension in length and thickness of the fibres due to wound swelling would open up the fibre micropores , thus enabling release of the wound - healing component to counteract the initial swelling . other miscellaneous applications are : fire - retardant ( fr ) fibres — due to incorporating fr component in pores of fibre by extending fibre during processing and then entrapping fr component by closing up pores due to release of extension after processing ; drug - delivery fibrous materials — similar to fr fibres where drug molecules / particulates are entrapped within fibres and subsequently released by extending fibres to open up pores ; other fibres which need to contain an additional component within the pores ( e . g . dye molecules for dyeability ); composite fibres — in which one or more components are auxetic fibres ( e . g . winding a dyeable fibre around an auxetic fibre in order to produce a fibre having benefits due to auxetic effect and also dyeability property ); fibrous seals — to exploit advantages due to auxetic property in seal and gasket applications . it is of course to be understood that the invention is not intended to be restricted to the details of the above embodiment which are described by way of example only .