|Número de publicación||US3920362 A|
|Tipo de publicación||Concesión|
|Fecha de publicación||18 Nov 1975|
|Fecha de presentación||11 Feb 1974|
|Fecha de prioridad||27 Oct 1972|
|Número de publicación||US 3920362 A, US 3920362A, US-A-3920362, US3920362 A, US3920362A|
|Inventores||Rexford H Bradt|
|Cesionario original||Jeffers Albert L|
|Exportar cita||BiBTeX, EndNote, RefMan|
|Citas de patentes (4), Citada por (68), Clasificaciones (11)|
|Enlaces externos: USPTO, Cesión de USPTO, Espacenet|
United States Patent n91 Bradt A FILAMENT FORMING APPARATUS WITH SWEEP FLUID CHANNEL SURROUNDING SPINNING NEEDLE  Inventor: Rexford II. Bradt, Claypool, Ind.
 Assignee: Albert L. Jelfers, Fort Wayne, Ind.
 Filed: Feb. 11, 1974  Appl. No.: 440,983
Related us. Application Data  Division of Ser. No. 301,611, Oct. 27, 1972, abandoned, which is a continuation-in-part of Ser. No. 96,305, Dec. 9, 1970, abandoned.
UNITED STATES PATENTS l/l970 Wagner et al. 425/72 Nov. 18, 1975 3,649,232 3/1972 Battigelli 425/7 X 3,649,233 3/1972 Battigelli... 425/7 X 3,649,234 3/1972 Charpentier 425/7 X  ABSTRACT A congealable synthetic material, for example, a melted thermoplastic, is formed into a filament by causing its removal in a fine stream from the tip of a pointed solid element to the surface of which the congealable material is fed at a controlled rate. The removal of the congealable material from the point of the pointed element is effected by directing a stream of fluid along the element toward the point while the fluid attenuates the withdrawn filament before it congeals. After leavingtlae point of the element, the material of the filament congeals, or is congealed, to form a dimensionally stable fiber or filament.
7 Claims, 16 Drawing Figures U .S. Patent Nov. 18, 1975 Sheet 1 of4 46 18,4 REXFOR D l-i g liDT US. Patent Nov. 18, 1975 Sheet20f4 3,920,362
\ DRIVE MEANS- N. R m R mB N N. M N H M A R O 7 w v R /m I O l 7//./ 0 w y 0 9 6 9 2 9 7 9 Sheet 4 of 4 U.S. Patent Nov. 1 8, 1975 INVENTOR REXFORD H. BRADT ATTORNEYS FILAMENT FORMING APPARATUS WITH SWEEP FLUID CHANNEL SURROUNDING SPINNING NEEDLE RELATED APPLICATION The present application is a division of my co-pending application, Ser. No. 301,61 1, filedOct. 27, 1972 entitled APPARATUS AND PROCESS FOR FORM- ING AND USING PLASTIC FIBERS, now abandoned, which application was a continuation-in-part of my copending application Ser. No. 96,305, filed Dec. 9, I970 and now abandoned.
BACKGROUND OF THE INVENTION Continuous synthetic fibers, or filaments, such as have been used in the textile industry have commonly been produced in one of two different ways. In one way a normally viscous material, such as a modified cellulose, for example, is forced through a spinneret and the emerging discrete streams are chemically treated to congeal the material and thereby form it into continuous filaments. In the other way, a thermoplastic resin is liquified, as by melting or dissolving it in an appropriate solvent, and forcing it through a spinneret, and the emerging discrete streams congeal on cooling to form filaments. The latter method also has been used to form continuous filaments of glass adapted for various uses.
There are several disadvantages inherent in these methods. Production rates are limited, and the fine openings in the spinneret have a tendency to clog or plug up with material, thereby requiring either a new spinneret or a great deal of effort to correct the situation. It is also very difficult to make discontinuous, or short, fibers with any high degree of uniformity.
Inorganic woolsT for uses as heat insulation have been produced by treating a stream of molten slag, glass, or the like with a high-velocity stream of air or gas which shatters the molten material into fine fibers. Fibers so produced lack uniformity and frequently are characterized by beaded ends rendering them unsuitable for certain uses. Glass wool has also been produced by feeding a glass rod into a high velocity, turbulent gas flame which both melts the glass and shatters .the melt into fibers. Fibers produced in these ways have wide variations in size and lengths.
It has further been proposed to create continuous fibers or filaments by drawing them under tension from points on the uninterrrupted surface of molten baths of glass. Such a method is disclosed in U.S. Pat. No. 2,235,352 to Bates. According to the Bates disclosure, the locations on the bath surface from which the fibers are drawn are determined initially by use of a horizontally extending element the upper edge of which is serrated in effect. This element is first immersed in the bath to submerge the serrations and then raised to bring the serrations above the glass level. Once the drawing of filaments from the serrrations has started, the serrrated element is lowered beneath the bath surface and tension in the filaments continues to draw them from the bath. One drawback to this method is that the size and length of the fibers cannot be closely controlled, as they are formed from an excess pool of material, not a metered feed. 7
It is, therefore, an object of this invention to provide an apparatus by which liquid congealable materials can be formed into fibers with a high degree of uniformity in length and cross-section and under conditions capaduction rates SUMMARY OF THE INVENTION This invention relates to the production of filaments or fibers by causing congealable liquid material to leave the tip of a pointed element to the outer surface of which the liquid is supplied and to products of various types made from such fibers or filaments. The liquid material may be either a molten thermoplastic; a solution of suitable material; or a normally liquid material such as a modified cellulose; or an incompletely polymerized plastic convertible by heat and further polymerization into a stronger thermoplastic or into a thermoset. After leaving the point, the fibers are congealed by subjecting them to an atmosphere with the appropriate congealing properties. The thermoplastic may be congealed simply by cooling; the dissolved material by evaporation of the solvent; the modified cellulose by heat or chemical treatment; and the incompletely polymerized plastic by a sprayed catalytic fog.
In preferred forms of my invention the congealable material is supplied in flowable form and at a controlled rate to a pointed element, hereinafter called a spin-off-point while a stream of fluid, preferably gaseous, sweeps the material to the tip of the point and therefrom as a fine stream congeable into a fiber or filament. The fluid stream also attenuates the drawn off filament before it congeals. The fibers may be continuousi'or discontinuous. The length of the discontinuous fibers as well as the tapering of their end portions may be controlled by regulating the supply of liquid material to the spin-off point. By pulsing or controlled starving of the liquid feed, discontinuous fibers of a specific length may be formed. I
By the use of supplemental streams of fluid or gas playing on the congealing or fully congealed filament, various effects may be produced. If the supplemental fluid stream flows in the same direction as the sweep fluid, tension can be introduced into the congealing filament to stretch orient it and promote its congealing in a straight form. If the supplemental fluid stream flows in the opposite direction and strikes the forming filament at an appropriate point, crimping in the finished from a congealable liquid by an apparatus comprising a circular rotatable head fitted-with a plurality of spin-off points located about its periphery and all pointed-in the same circumferential direction. As the head is .rotat'ed, centrifugal forces feed the liquidto the points, and tangentially blown sweep fluid, flowing in the same circumferential direction as the spin-off points are point ing, sweeps discontinuous incipent fibers therefrom, and the congealed fibers become combined and intertwisted by the swirling fluid to form a continuous thread, yarn, or the like.
Filaments may be felted or otherwise agglomerated to produce bats, sheets, or the like in a wide variety of sizes and characteristics. In materials so formed, the degree of cohesion holding the individual fibers in place can be controlled by controlling the extent to which filaments have congealed before being brought into contact with other filaments. If cohesion in the felted sheet is to be avoided, complete congealing of the fibers before disposition may be effected by treatment with a gas or fog containing a release agent.
BRIEF DESCRIPTION OF THE DRAWINGS The accompanying drawings illustrate the invention. In such drawings:
FIG. 1 is a vertical section showing fiber spinning apparatus for producing and twisting fibers;
FIG. 2 is a section on the line 2-2 of FIG. 1;
FIG. 3 is a sectional view on an enlarged scale illustrating a detail of construction;
FIG. 4 is a sectional view of a device for forming single filaments;
FIG. 5 is a section on the line 55 of FIG. 4;
FIG. 6 is a front elevation of an apparatus containing a circular array of spin-off points;
FIG. 7 is a section on the line 7-7 of FIG. 6;
FIG. 8 is a front elevation of an apparatus with a linear array of spin-off points;
FIG. 9 is a section on the line 9--9 of FIG. 8.
FIG. 10 is a fragmental section showing apparatus for making fibers from a rod of meltable material;
FIG. 11 is a side elevational depicting apparatus for intertwisting into a thread or yarn fibers formed therein;
FIG. 12 is a diagrammatic showing of a system for felting fibers into a sheet or bat;
FIG. 13 is a representation, partially diagrammatic, of a system for producing a faced bat;
FIG. 14 is a diagrammatic showing of apparatus for producing multi-layered material;
FIG. 15 is an axial section showing an embodiment in which filaments are spun from an annular series of spinoff points; and
FIG. 16 is a cross-section on the line 16l6 of FIG.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS casing 10 and supports therein a circular hollow head '18. The peripheral wall of the head 18 is provided with a series of radial holes 19 (FIG. 3) each of which has in its outer end a screw threadedly mounted discharge fitting 20. Each of the fittings 20 carries a tangentially projecting spin-off point 26 to which the congealable material is supplied at a region spaced from the point via a passage 22 from the hole 19. The fittings 20 are so oriented about the axes of the holes 19 that the points 26 all project in the same circumferential direction, which is opposite to the direction of head rotation, indicated by arrow 18a in FIG. 2.
Fluid, such as air, or other gas, is supplied to the casing 10 through a tangential inlet conduit 24 in about the plane of the head 18 and so arranged that the gas introduced through it will swirl in thecasing in a direction opposite to that in which the head 18 rotates. The swirling gas acts on liquid emerging from each passage 22 to cause the liquid to flow along the surface of the respective fittings 20 to the points 26 and to be carried therefrom as fine streams each of which, when congealed, will constitute a fiber.
The rate at which the congealable liquid is supplied to the extreme tip of the spin-off point is low enough that the fibers produced are discontinuous as explained 4. below, and short relative to the size of the head 18. The fibers from the several points become entrained in the swirling gas, which acts to combine and intertwist the fibers into a continuous thread that can be withdrawn from the casing through the opening 14.
An arrangement for forming a single filament in accordance with my invention is shown in FIGS. 4 and 5. In this structure a nozzle 28 is fitted interiorly with a point support 30 in which is mounted a spin-off point in the form of a solid needle-like member 32. The member 32 has a diameter less than that of the orifice of the nozzle 28 and extends forwardly through and beyond such orifice. A plurality of grooves 36 (FIG. 5) in the periphery of the support 30 permit congealable liquid material to flow past the support to the nozzle orifice and thence along the outer surface of the spin-off point 32 to the pointed tip end 38 thereof.
The nozzle 28 and the projecting spin-off point extend from the rear into a converging gas-passage 42 through which fluid, gas, for example, flows from a supply conduit 43 to sweep liquid material on the spin-off point to and off the tip 38 as a fine stream which, on congealing, will become a filament. If the feed of liquid to the spin-off point is adequate, the filament can be continuous, but at lower feed rates, the sweep fluid passing through passage 42 may intermittently sweep the tip 38 of the spin-off point clean, thus interrupting filament-generation and causing the production of discontinuous fibers.
As shown in FIG. 4, the body 46 in which sweep fluid passage 42 is formed contains a plurality of additional fluid passages disposed in forwardly converging relation around the passage 42, and terminating at their forward ends in discharge orifices 48 directed to discharge jets of fluid obliquely against the filament or aginst the fine liquid stream that is to congeal into a filament or fiber. The function performed by the jets from the orifices 48 depends upon several factors. If the congealable material is melted thermoplastic, jets having a temperature below the melting point of the material will further congeal and create tension in the congealing material to provide some stretch orientation and overcome any tendency of the still soft filament to contract as a result of its plastic memory. Further, the jets from the orifices 48 may contain catalysts or reagents necessary to effect chemical congealing of the liquid material leaving the spin-off point. Whatever material is used, if the jets do not participate in the congealing or setting of the filament, they still can be used to stretch, stabilize and refine the material.
By using an annular series of nozzles 48 so oriented that the jet from each has a tangential velocity-component about the axis of the spin-off point, a twist will be imparted to the filament formed. Such twist imparts to the filament an appearance somewhat different from that of an untwisted filament. A similar series of similarly disposed nozzles about the axis of an annular series of spin-off points such as shown in FIGS. 6 and 7, and below described, will cause the several filaments respectively propelled from the points to be intertwisted as they are formed. Twisting effects, either on a single filament, or on a group of parallel filaments, can also be produced by an annular series of orifices such as shown in FIG. 4 and progressively pulsing the gas discharged from successive nozzles.
An apparatus comprising a series of spin-off points arranged in a circle is shown in FIGS. 6 and 7. The spinoff points 54 are located respectively in axially extending grooves 56 formed in the circumferential surface of a cylindrical member 58. Each groove 56 is open at its front and rear ends, and the spin-off points project forwardly beyond the front ends of the grooves. The member 58 is snugly received in a central opening in an internal annular flange 60 in a hollow, cylindrical body 62. Surrounding the member 58 in rear of flange 60 is an annular plenum chamber 63 to which fluid under pressure is supplied through a conduit 64 and from which the fluid escapes in the axial direction through the grooves 56. The liquid material to be spun is supplied to the grooves near their rear ends through passages 66 in the member 58 and is carried by the escaping fluid to the tips of the spinning points.
The fiber formation in this case is like that hereinbefore described in that the congealable material, under the control of the sweeping action of the fluid supplied from chamber 63, encases the tip and sweeps the film of congealable material along the outer surface thereof and off the point to propel forwardly off each spin-off point a fine, congealable stream.
A second multiple spin-off point arrangement, in which the several spin-off points are disposed in a common plane, is shown in FIGS. 8 and 9. The body comprises three portions72, 74 and 76 to facilitate the provision of the necessary internal cavities. Each of the spin-off points is the outer end portion of a solid member 78 fitted in a screw 80 which is received in the rear body portion 76. Congealable material is supplied from pipe 82 into supply chamber 84 which is common to all the spin-off point members in the apparatus Fowardly of this supply chamber 84, and separated therefrom by a wall 85, is a chamber 86 which is supplied with pressurized sweep fluid through a pipe 88. The members 78 extend through holes of larger diameter in the wall 85 and across the chamber 86, their front ends, which constitute the spin-off points proper, projecting into nozzles 89 provided on body portion 72. The length and diameter of the fibers produced are affected by the longitudinal position and the general form of the spin-off points 78 A variation upon my spin-off filament apparatus is shown in FIG. 10. A rod 90 of a thermoplastic material with a pointed conical end 92 is positioned within a chamber 94 with its pointed end entering an outlet nozzle 95. Fluid entering the chamber 94 via inlet pipe 96 is hot enough to melt the material on the surface of the rod, and, as the fluid flows along such surface and exits through nozzle 95, it causes the melted material to flow on the as yet unmelted core to the point thereof from which it leaves as a fine stream 97 congealable into a filament upon cooling. The point 92 is self-rejuvenating as long asthe rod is steadily fed into the hot sweep fluid at an appropriate rate. The longitudinal position of the tip 92, the velocity of sweep fluid and the temperature thereof determine the length and diameter of the filament to be swept. As long as the feed of the unmelted rod 90 is balanced against the amount of material being swept from the point 92, continuous fibers may be formed at a below turbulent sweep fluid speed which permits a high degree of uniformity in the fibers diameter. Discontinuous fibers may be produced by intermittently interrupting the feed of the rod or pulsing the sweep fluid. If the rod 90 is of a thermoplastic resin it may be formed by an extruder and fed directly therefrom and thereby into chamber 94 through a suitable guide channel.
Apparatus for producing a thread or yarn from discontinuous fibers formed from spin-off points is shown in FIG. 11. Typically, melted thermoplastic or other congealable material is placed in a hopper 98 and fed by an extruder 100 to a fiber forming device 104, which may be of the general type shown in FIGS. 6-7 and 89. Fluid under pressure supplied to this device 104 through intake 106 sweeps the spin-off points 108 of device 104 to form discontinuous incipient fibers delivered to a plenum chamber 110. The chamber 110 is supplied with fluid of the proper temperature and pressure through inlet pipe 112 to partially cool the incipient fibers. This is done to control the amount of cohesion between the respective fibers in the twisted thread or yarn to be formed.
The suspension of semi-cooled fibers then enters tangentially into an inverted conical chamber 114 generally of the form used in dust separators of the so called cyclone type. Fluid escapes from the chamber 114 through outlet conduit 1 16, and a whirlpool of fluid rotating at high speeds exists within the apparatus.
In the chamber 114, the fibers are twisted together into a thread-like or yarn-like form 118 which is pulled from the lower end 120 of the chamber 1 14 by a pair of pulling rollers 122 driven by drive means 126. A set of tension rollers 124, driven at a greater speed than the pulling rollers 122, applies tension to the thread for sile loading at all.
" The felting system depicted in FIG. 12 may incorporate, as indicated at 134, any of the spin-off point devices shown in FIGS. 1 through 9, using a molten thermoplastic 131 as the filament material. An annular accelerating ring or collar may surround the filament or filaments emerging from the device 134 to discharge fluid against those filaments in a direction such as to stretch them and assure their impingement upon a rotating and reciprocating drum 136. As this drum 136 is moved axially back and forth, as shown by the arrows, it is slowly rotated, steadily or incrementally, as the impinging fibers form a mat or sheet on its surface. The fineness of the fibers produced, along with the speed with which the drum rotates and reciprocates, determine the nature of the felted material produced.
The surface of drum 136 can also be used to impart a texture or design to the formed sheet. For example, if a screen mesh constitutes or is placed on the surface of the drum 136 the resultant sheet will have a screen mesh texture. The use of any other embossed base will likewise cause the sheet to have a corresponding appearance. By first coating the drum 136 with a jellied vinyl plastic and impinging the hot fibers thereon, a reinforced web-backed vinyl sheet can be produced in a one step, single machine operation.
A variation of this apparatus is shown in FIG. 13. Here, two rotating drums 138 and .140 feed two strips or sheets 142 and 144 of fabric, forxample, in parallel spaced relation as a layer of hot f "d filaments formed by a spin-off point apparatus 146 eposited between 7 them. This sandwiched hot layer of thermoplastic fibers adheres to and bonds together the two fabrics 142 and 144 and can provide a permanent insulating layer between them.
In another felting apparatus, shown in FIG. 14, a conveyor belt 148 driven by a drive means 150 on rollers 152 and 154 can be used as the impinging target or to carry an impinging target. This target, as above, may be of any material or may have any surface texture which is desired to impart to the felted sheet to be formed. Head support 156 carries two spin-off heads 158 and 160 on guide member 162 extending transversely of belt 148. Conveyor belt 148 is moved in the direction shown and the head support 156 is moved back and forth on its guide 162 to deposit the filaments across the belt. In the absence of any auxiliary fluid jet, or jets, serving to deflect laterally the filaments discharged from a spin-off head, such filaments will be deposited in generally parallel relationship. The angle between those generally parallel filaments and the direction in which the belt 152 moves is largely determined by the orientation of the head relative to the path of belt movement, but will be influenced to an extent by the relation between the speed of belt movement and the speed of movement of the support 156. By depositing on a layer of filaments oriented in one direction a second layer in which the filaments are oriented in another direction an appearance simulating that of a woven fabric can be created. Where a plurality of heads are used variations in appearance can be created by supplying the heads with materials of different colors. In felted' sheets simulating fabrics in appearance successively deposited layers of filaments will be bonded together either by the cohesiveness of still soft filaments or by an adhesive sprayed on or otherwise applied.
FIGS. and 16 illustrate a spin-off head which, like those of FIGS. 6-7 and 8-9, simultaneously produces a plurality-of filaments or fibers. This head comprises a hollow circular casing 160 which tapers at its front end to a nozzle-like portion 162. Mounted axially within the nozzle 162 is a tubular sleeve 164 of smaller diameter than the nozzle and providing an annular opening 166. At its front end, the sleeve 164 is serrated to provide an annular series of spin-off points 168 and at its rear end it terminates in a funnel-like flange 170. On the axis of the head and spaced rearwardly from the rear end of flange 170 is the outlet of a conduit 172 through which is supplied the material to be spun Axially between the flange 170 and the outlet of conduit 172, the interior of casing 160 communicates with a tangentially discharging conduit 174 for sweep fluids, such as air or gas.
In operation of the device shown in FIGS. 15 and 16, fluid such as air, or other gas, entering the casing 160 tangentially swirls therein and escapes from the casing through the sleeve 164 and annular opening 166 thereby sweeping the spin-off points 168. The stream 176 of more or less viscous material emerging from conduit 172 does not atomize or otherwise break up and, caught in the swirling air, impinges upon the inner surface of the sleeve 164 to be swept forwardly to the spin-off points 168 and therefrom by the fluid escaping from the sleeve and around it through opening 166.
In any of the various forms of spin-off point devices above described the parameters obtaining will depend upon the type of congealable material employed and upon the type of filaments or fibers desired. Temperatures at and adjacent the spin-off points are to be controlled so as to insure that the material to be spun is of 8 appropriate viscosity for spinning but not high enough to damage the material. For example, in spinning fibers or filaments from polypropylene, the material is ordinarily supplied to the spin-off device at a temperature from about 400 to about 600F. Sweep fluid, air, or such other gas, ordinarily would have a temperature about that of the material or somewhat higher, although in some cases using thermoplastics supplied at relatively high temperature, it may be advisable that the sweep fluid be substantially cooler than the material to be spun. With thermoplastics, temperatures of course affect viscosities; the spinning of fine filaments requires lower viscosities than does the spinning of coarser filaments.
Ambient temperatures beyond the spin-off points may be of importance. With thermoplastics, if the incipient filaments are allowed to cool slowly while not maintained under tension, plastic memory may cause them to contract, or snap back, into pretzel-like snarls. This may be prevented, even in the absence of tension, by quick cooling produced, for example, by a cooling fog or mist. In some instances, as when the spun material is of a character such that its congealing requires heat-curing or drying, ambient temperatures may be higher than spinning temperature as referred to here may be simply the temperature of the space into which the sweep fluid carries spun fibers or the temperature of auxiliary fluid discharged against filaments after they have left the spin-off points. Ambient temperatures may also be significant in felting operations and other situations where the incipient filaments are deposited on other filaments, for in such situations temperature can determine the extent to which successively deposited filaments cohere. Coherence, or its absence, between successively deposited fibers may also be controlled by spraying the fibers with a liquid adhesive or with a release agent.
Sweep fluid velocities and nature of flow thereof can effect the filaments produced. Laminar flow of sweep fluid promotes the formation of straight filaments, while turbulent flow tends to produce crimped filaments. Crimped filaments can also be produced if the sweep fluid decelerates too rapidly before the filaments have set. Velocity of sweep fluid at a spin-off point affects the diameter of filament produced. For instance, raising from about 12 psi to about 25 psi the pressure of sweep fluid supply when air or gas is used, and thereby increasing the velocity of the sweep fluid at the spin-off has reduced filament diameter from 0.0l0-0.0l5 inch to 0.0005-0.00linch.
It has been pointed out above that the relation between sweep fluid velocity and the rate at which the spin-off point receives the congealable material affects the length of fibers or filaments produced. Specifically, the sweep fluid velocity can be made high enough that it intermittently strips the spin-off point completely and so terminates continuing lengthening of the filament being produced. As the feed of liquid material to the spin-off point continues, filament generation will resume when enough of the liquid has accumulated on the point. The length of the discontinuous fibers produced in this manner decreases as the velocity of the sweep fluid increases without a related increase in the rate of liquid supply. The fibers are especially well suited to being spun into thread, as they taper toward their ends. The tapered ends of fibers contribute to imparting a smooth feel to a felted sheet, yarn, or fabric.
Although the above description of illustrated embodiments all contemplate the use of air or other gas as the spinning fluid, there are cases in which the spinning can be performed by a liquid. For example, where the congealable material is a modified cellulose the spinning fluid could be a liquid of the type used in the production of rayon to congeal the liquid streams emerging from a conventional spinneret.
Instead of sweeping the congealable material from a spin-off point with a fiber spinning fluid, the material can, if adequately viscous, be pulled from the tip of the spin-off point by a reel or like device. It will of course be understood that, in this method, the material leaving this spin-off point must be substantially congealed by the time it reaches the reel. Owing to its viscosity, the liquid material on the point will be drawn to the tip of the point to replace that pulled from the tip by the reel. The relation between the speed of the reel and the rate at which material is supplied to the point determines the size of the filament produced.
In every example given above, the spinning element is solid to the extent that it has an outwardly facing surface which tapers in to a point at one axial end of the element and from which point the liquid, or flowable, material is drawn to form a filament and which filament is then attenuated and caused to congeal. The fluid which sweeps the material along the spinning element to the point end thereof and which draws the material off the spinning point as a filament and conveys it away from the point while attenuating the filament is usually a gas, air, for example.
As has been mentioned above, the method and apparatus of the present invention is applicable to a variety of synthetic materials. Among the materials, which can be softened, or liquified by heat and which congeal upon cooling are polypropylene, polyethylene, certain of the polyvinylchlorides and polyamids.
Among the materials which are rendered flowable by a solvent and which congeal by evaporation of the solvent therefrom are the acrylics and certain polyvinylchlorides.
An example of the material which congeals by dataly-tic action is a polyester resin or a viscose in which the spinning is preceded by an acid bath and wherein the sweep air, or the air which impinges on the filament after it is attenuated, contains an acidic precipitant.
An example of a material which congeals by chemical action supplied to the material in the sweep fluid, or in fluid or air impinging on the filament is phenol-formaldehyde. In this case, an acidic vapor is employed to effect the congealing which could, for example, be hydrochloric acid. Alternatively, a fogconsisting of or containing evaporated phosphoric acid could be employed. At least some of the resorcinol formaldehyde resins also fall in this classification.
, In every case, fine nozzles to form filaments are eliminated, as well as the known problems attendant thereto. Filaments of controlled uniform diameter free of beaded ends are formed at a rapid rate and can be individually twisted, twisted together in groups, matted, or otherwise processed.
Modifications may be made within the scope of the appended claims.
What is claimed is:
1. An apparatus for making filaments of uniform diameter and free of beaded ends from a congealable liquid material comprising, in combination, a spinning element in the shape of an elongated needle having a lon- I gitudinal axis and an outer surface facing outwardly away from said axis and tapering inwardly in one axial direction of said spinning element to a spinning point, nozzle means for supplying congealable liquid material to substantially the entire outer surface of said spinning element at a region thereof which is axially spaced from said spinning point, wall means substantially surrounding the spinning element in radially spaced relation thereto and forming a channel surrounding and extending axially of said spinning element for the flow of sweep fluid in one axial direction along said spinning element and on beyond the spinning point in said one axial direction so that fluid impelled in said axial direction within the channel will cause the liquid material to flow around the spinning element to the spinning point, whereby the fluid will draw the liquid material from the spinning point as a filament and will convey the filament away from the spinning point while attenuating the filament.
2. An apparatus according to claim 1 wherein the wall means includes at least one additional fluid passage adjacent the channel and having a discharge orifice positioned to discharge fluid against the filament being formed.
3. An apparatus according to claim 1 in which support means is provided for mounting the spinning element within said nozzle means. I
4. An apparatus according to claim 3 wherein the spinning element has a diameter less than that of the orifice of the nozzle and extends forwardly through and beyond the orifice of the nozzle.
5. An apparatus according to claim 1 including an annular series of nozzle means having fluid discharge orifices disposed around the axis of the spinning point so that fluid flowing from the discharge orifices will cause F lation.
|Patente citada||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US3543332 *||28 Jun 1968||1 Dic 1970||Celanese Corp||Apparatus for producing fibrous structures|
|US3649232 *||12 Mar 1969||14 Mar 1972||Saint Gobain||Method and apparatus for production of fibers from thermoplastic materials, particularly glass fibers|
|US3649233 *||19 Mar 1969||14 Mar 1972||Saint Gobain||Method of and apparatus for the production of glass or other fibers from thermoplastic materials|
|US3649234 *||10 Jun 1969||14 Mar 1972||Saint Gobain||Method and apparatus for production of fibers from thermoplastic materials, such as glass, rock, slag or the like|
|Patente citante||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US4025593 *||9 Jun 1975||24 May 1977||Solvay & Cie||Fabrication of discontinuous fibrils|
|US4197063 *||28 Jul 1978||8 Abr 1980||Imperial Chemical Industries Limited||Spinning fibres|
|US4226576 *||18 Ene 1978||7 Oct 1980||Campbell Soup Company||Protein texturization by centrifugal spinning|
|US4321026 *||21 Mar 1979||23 Mar 1982||Werner & Pfleiderer||Device for granulating plastic strands|
|US4323524 *||9 May 1980||6 Abr 1982||Imperial Chemical Industries Limited||Production of fibres|
|US4375446 *||1 May 1979||1 Mar 1983||Toa Nenryo Kogyo Kabushiki Kaisha||Process for the production of a nonwoven fabric|
|US4455761 *||12 Nov 1981||26 Jun 1984||Terhune Robert D||Pneumatic polymer eductor conveyor dryer|
|US4969602 *||29 Sep 1989||13 Nov 1990||Nordson Corporation||Nozzle attachment for an adhesive dispensing device|
|US5065943 *||6 Sep 1990||19 Nov 1991||Nordson Corporation||Nozzle cap for an adhesive dispenser|
|US5160746 *||18 Jul 1991||3 Nov 1992||Kimberly-Clark Corporation||Apparatus for forming a nonwoven web|
|US5165940 *||23 Abr 1992||24 Nov 1992||E. I. Du Pont De Nemours And Company||Spinneret|
|US5169071 *||13 Ago 1991||8 Dic 1992||Nordson Corporation||Nozzle cap for an adhesive dispenser|
|US5238190 *||16 Jun 1992||24 Ago 1993||Nordson Corporation||Offset nozzle assembly|
|US5478224 *||4 Feb 1994||26 Dic 1995||Illinois Tool Works Inc.||Apparatus for depositing a material on a substrate and an applicator head therefor|
|US5667749 *||2 Ago 1995||16 Sep 1997||Kimberly-Clark Worldwide, Inc.||Method for the production of fibers and materials having enhanced characteristics|
|US5711970 *||2 Ago 1995||27 Ene 1998||Kimberly-Clark Worldwide, Inc.||Apparatus for the production of fibers and materials having enhanced characteristics|
|US5807795 *||2 Jun 1997||15 Sep 1998||Kimberly-Clark Worldwide, Inc.||Method for producing fibers and materials having enhanced characteristics|
|US5811178 *||15 Nov 1996||22 Sep 1998||Kimberly-Clark Worldwide, Inc.||High bulk nonwoven sorbent with fiber density gradient|
|US5882573 *||29 Sep 1997||16 Mar 1999||Illinois Tool Works Inc.||Adhesive dispensing nozzles for producing partial spray patterns and method therefor|
|US5902540 *||8 Oct 1996||11 May 1999||Illinois Tool Works Inc.||Meltblowing method and apparatus|
|US5904298 *||14 Abr 1997||18 May 1999||Illinois Tool Works Inc.||Meltblowing method and system|
|US6001303 *||19 Dic 1997||14 Dic 1999||Kimberly-Clark Worldwide, Inc.||Process of making fibers|
|US6051180 *||13 Ago 1998||18 Abr 2000||Illinois Tool Works Inc.||Extruding nozzle for producing non-wovens and method therefor|
|US6074597 *||20 Feb 1999||13 Jun 2000||Illinois Tool Works Inc.||Meltblowing method and apparatus|
|US6197406||16 Mar 2000||6 Mar 2001||Illinois Tool Works Inc.||Omega spray pattern|
|US6200635||31 Ago 1998||13 Mar 2001||Illinois Tool Works Inc.||Omega spray pattern and method therefor|
|US6378782||29 Oct 1999||30 Abr 2002||Nordson Corporation||Method and apparatus for applying a controlled pattern of fibrous material to a moving substrate|
|US6461430||16 Mar 2000||8 Oct 2002||Illinois Tool Works Inc.||Omega spray pattern and method therefor|
|US6540831||16 Abr 1999||1 Abr 2003||Nordson Corporation||Method and apparatus for applying a controlled pattern of fibrous material to a moving substrate|
|US6602554||14 Ene 2000||5 Ago 2003||Illinois Tool Works Inc.||Liquid atomization method and system|
|US6680021||20 Oct 2000||20 Ene 2004||Illinois Toolworks Inc.||Meltblowing method and system|
|US6890167||18 Mar 2000||10 May 2005||Illinois Tool Works Inc.||Meltblowing apparatus|
|US7118698||5 Abr 2004||10 Oct 2006||E. I. Du Pont De Nemours And Company||Rotary process for forming uniform material|
|US7621731||13 Feb 2006||24 Nov 2009||E.I. Du Pont De Nemours And Company||Rotary process for forming uniform material|
|US7786034||14 Mar 2006||31 Ago 2010||E.I. Du Pont De Nemours And Company||Rotary process for forming uniform material|
|US7798434||13 Dic 2006||21 Sep 2010||Nordson Corporation||Multi-plate nozzle and method for dispensing random pattern of adhesive filaments|
|US8074902||14 Abr 2008||13 Dic 2011||Nordson Corporation||Nozzle and method for dispensing random pattern of adhesive filaments|
|US8435600||3 Nov 2011||7 May 2013||Nordson Corporation||Method for dispensing random pattern of adhesive filaments|
|US8641960 *||29 Sep 2010||4 Feb 2014||The United States Of America, As Represented By The Secretary Of Agriculture||Solution blow spinning|
|US8647540||7 Feb 2012||11 Feb 2014||Fiberio Technology Corporation||Apparatuses having outlet elements and methods for the production of microfibers and nanofibers|
|US8647541||7 Feb 2012||11 Feb 2014||Fiberio Technology Corporation||Apparatuses and methods for the simultaneous production of microfibers and nanofibers|
|US8650915 *||26 Ago 2010||18 Feb 2014||Johns Manville||Processes and systems for making inorganic fibers|
|US8658067||7 Feb 2012||25 Feb 2014||Fiberio Technology Corporation||Apparatuses and methods for the deposition of microfibers and nanofibers on a substrate|
|US8709309||7 Feb 2012||29 Abr 2014||FibeRio Technologies Corporation||Devices and methods for the production of coaxial microfibers and nanofibers|
|US8721319||16 Mar 2009||13 May 2014||Board of Regents of the University to Texas System||Superfine fiber creating spinneret and uses thereof|
|US8777599||7 Feb 2012||15 Jul 2014||Fiberio Technology Corporation||Multilayer apparatuses and methods for the production of microfibers and nanofibers|
|US8778240||7 Feb 2012||15 Jul 2014||Fiberio Technology Corporation||Split fiber producing devices and methods for the production of microfibers and nanofibers|
|US8826802 *||28 Oct 2011||9 Sep 2014||Gruppo Cimbali S.P.A.||Replaceable end-piece for a vapour nozzle of a coffee machine|
|US8828294||19 Jun 2012||9 Sep 2014||Board Of Regents Of The University Of Texas System||Superfine fiber creating spinneret and uses thereof|
|US8870559 *||28 Nov 2011||28 Oct 2014||Toyota Boshoku Kabushiki Kaisha||Melt spinning apparatus and melt spinning method|
|US9394627||15 Oct 2015||19 Jul 2016||Clarcor Inc.||Apparatuses having outlet elements and methods for the production of microfibers and nanofibers|
|US20040219345 *||5 Abr 2004||4 Nov 2004||Armantrout Jack Eugene||Rotary process for forming uniform material|
|US20090269429 *||16 Mar 2009||29 Oct 2009||Karen Lozano||Superfine fiber creating spinneret and uses thereof|
|US20100291252 *||30 Jul 2010||18 Nov 2010||Taiwan Textile Research Institute||Method of Producing Ultra Thin Chitosan Fibers and Non-Woven Fabrics|
|US20100319404 *||26 Ago 2010||23 Dic 2010||Harley Allen Borders||Processes and systems for making inorganic fibers|
|US20120104038 *||28 Oct 2011||3 May 2012||Gruppo Cimbali S.P.A||Replaceable end-piece for a vapour nozzle of a coffee machine|
|US20120139153 *||28 Nov 2011||7 Jun 2012||Toyota Boshoku Kabushiki Kaisha||Melt spinning apparatus and melt spinning method|
|CN100429336C||5 Abr 2004||29 Oct 2008||纳幕尔杜邦公司||Rotary process for forming uniform material|
|CN104294383A *||31 Oct 2014||21 Ene 2015||苏州大学||Airflow rotary table spinning device used for preparing nanofiber|
|CN104294383B *||31 Oct 2014||23 Nov 2016||苏州大学||一种应用于制备纳米纤维的气流转盘纺丝装置|
|DE2810535A1 *||10 Mar 1978||14 Sep 1978||Ici Ltd||Verfahren zum zentrifugenspinnen von fasern aus einem fluessigen formaldehydharz|
|EP0401829A2 *||7 Jun 1990||12 Dic 1990||Kimberly-Clark Corporation||Process and apparatus for forming fibers|
|EP0401829A3 *||7 Jun 1990||3 Jul 1991||Kimberly-Clark Corporation||Process and apparatus for forming fibers|
|EP0983797A3 *||5 Ago 1999||5 Feb 2003||Robatech AG||Method and device for applying an adhesive onto a product surface|
|EP2264230A3 *||5 Abr 2004||23 Mar 2011||E. I. du Pont de Nemours and Company||Rotary process for forming uniform material|
|WO2004090206A1 *||5 Abr 2004||21 Oct 2004||E.I. Dupont De Nemours And Company||Rotary process for forming uniform material|
|WO2012109242A2 *||7 Feb 2012||16 Ago 2012||Fiberio Technology Corporation||Devices and methods for the production of coaxial microfibers and nanofibers|
|WO2012109242A3 *||7 Feb 2012||6 Dic 2012||Fiberio Technology Corporation||Devices and methods for the production of coaxial microfibers and nanofibers|
|Clasificación de EE.UU.||425/72.2, 65/524, 425/7, 264/164, 65/506|
|Clasificación internacional||D01D5/18, D01D5/00|
|Clasificación cooperativa||D01D5/18, D01D5/00|
|Clasificación europea||D01D5/18, D01D5/00|