|Publication number||US3353211 A|
|Publication date||21 Nov 1967|
|Filing date||29 Dec 1965|
|Priority date||6 Jan 1965|
|Also published as||DE1934224U|
|Publication number||US 3353211 A, US 3353211A, US-A-3353211, US3353211 A, US3353211A|
|Inventors||Heijnis James W Ij|
|Original Assignee||American Enka Corp|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (9), Referenced by (19), Classifications (12)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Nov. 21, 1967 J. w. 1.1. HEIJNIS 3,353,211
SPINNERET ASSEMBLY Filed Dec. 29, 1965 2 Sheets-Sheet 2 .LZIZN'ZL'MAAQQ MM mama FEG.5
JAMES W. IJ. HEIJNIS BY AGENT United States Fatent ()fiFice 6 3,353,211 Patented Nov. 21, 1967 3,353,211 SPINNERET ASSEMBLY James W. 1 Heijnis, Arnhem, Netherlands, assigaor to American Enka Corporation, Euka, N.C., a corpora- 65- 6 Claims. (Cl. 188) ABSTRACT OF THE DISCLOSURE A spinneret pack assembly embodying means for improving heat conductivity and sealing when subjected to polymer hydraulic pressure comprising, an inlet piece or fill plug within the assembly housing having a molten polymer flow conduit leading into a horizontally disposed molten polymer distribution channel which splits the molten polymer into two distinct patterns of flow, said channel extending almost entirely around the circumference of the inner wall of the assembly housing with the width thereof gradually narrowing both in a downward and horizontal direction. Novel means is also provided for centering a plurality of filter screens within the housmg.
This invention relates to an apparatus for spinning artificial filaments; more particularly, the invention relates to an improved heat conducting spinneret pack assembly used in spinning filaments from thermoplastics.
In production of filaments from higher weight linear polymers, such as polyamides and polyesters, a melt of the polymer is usually fed to a spinneret pack assembly at very high pressure and at high temperatures from a conduit associated in some manner with a pressure screw mechanism or a metering pump. The spinneret pack assembly serves to prevent incompletely fused polymer, foreign matter, pigment aggregations, or aggregates of delustering materials or the like from reaching a spinneret plate which forms the polymer into filaments. To permit this, heated spinneret packs are conventionally used having a housing which is usually cylindrical in shape supporting and confining an inlet piece or fill plug, a series of filters, auxiliary devices such as melt distribution plates and supporting plates for a spinneret or spinneret plate through which the melt is extruded. The molten polymer is usually fed from the main feed conduit to the housing and through the sides thereof and the melt is further passed through a feed channel to the center of the inlet piece and is then centrally distributed downwardly the filter arrangement before being passed through the spinneret plate.
Disadvantages long associated with this type spinneret pack assemblies are that heat conduction between the heated housing to the melt in the center of the inlet piece is not satisfactory and air is sometimes entrained in the melt particularly at the beginning of the melt spinning process. Heat conductivity is a problem because of the distance between the interior of the housing sidewall and the continuously flowing molten polymer in the center of the inlet piece. Since the polymer does not directly flow along or across the primary heat conducting surface, uneven polymer heating and heat loss often occur. Air entrainment in the melt is a problem and is caused in these prior art devices primarily by methods used to pressure seal the apparatus to prevent polymer leakage. This problem is particularly great in spinnert packs which use a self-sealing expedient in an attempt to prevent undue polymer leakage from the spinneret assembly. In such a proposal, the inlet piece usually is spaced from the housing to permit movement therein. High pressures building up in these devices cause the piece to be pressed upwards to come in contact with a sealing ring which becomes deformed on contact with the piece. Uneven and fluctuating pressure acting on the element causes uneven deformation of the sealing ring and this leads to air seepage into the melt particularly in the clearance area between the inlet piece and the inner sidewall of the housing. Air gradually escapes from the spinneret plate in the form of small bubbles which cause filament breakage and results in yarn of inferior quality.
Accordingly, it is an object of this invention to provide a novel heat conducting type spinneret pack assembly which is used in spinning yarns and threads from polymeric substances.
Another object is to provide means which allow uniform heat distribution throughout the molten polymer passing through the novel spinning pack assembly.
A further object is to provide a novel spinning pack assembly wherein an inclusion of air with a molten polymer passing through the assembly is prevented.
In general, the above objects as well as additional advantages are obtained in accordance with this invention by providing Within the spinneret housing, an inlet piece or fill plug having a melt entry conduit and distribution channel of a novel configuration. The novel inlet piece of this invention has a conduit leading into a horizontally disposed melt distribution channel which causes the melt to be split into two individual flow patterns. Such design permits an exceptional uniform melt distribtuion over a heat conducting housing interior sidewall and to the additional assemblies positioned below the channel. It allows direct contact of the polymer with the heated housing and the prevention of included air in the formed polymer. Included air is prevented by the developed back pressure of the polymer flow to and within the distribution channel and its even pressure distribution to sealing means employed in the assembly.
The foregoing will become more apparent to those skilled in the art upon study of the following description taken in conjunction with the accompanying drawings, wherein:
FIGURE 1 shows, in longitudinal section, the spinneret pack assembly of the present invention showing a transverse melt filtration expedient;
FIGURE 2 is a section along the line 11-11 in FIG. URE 1;
FIGURE 3 is a section along the line IIIIII in FIGURE 1;
FIGURE 4 shows an additional embodiment, in which the polymer filtration takes place both in the transverse direction and in the longitudinal direction; and
FIGURE 5 shows an additional embodiment.
In FIGURE 1 the numeral 1 refers to the cylindrical housing, which can be heated in any known manner (not shown). Provided in housing 1 is a spinning pack assembly which comprises, from the top downwards, fill plug or inlet piece 2, a pack of filter screens or gauzes 3, support plate 4, and spinneret plate 5. Provided on the housing 1 is closure or cap member 6 (part of which being shown), which can be fastened in any known manner, for example by bolts, which are indicated by a line 7. When the bolts are tightened, the melt spinning apparatus will be completely sealed by pressure of the polymer being translated to scaling rings 8, 9, and 10. Into closure 6 opens the main polymer feed conduit 11, which is connected to channel 12 in inlet piece 2. Near the circumference of inlet piece 2, channel 12 opens directly into the horizontally disposed distribution channel 13, which encircles the assembly. The polymer melt, after entering distribution channel 13 from channel 12 at its sole port of entry, splits into individual streams and completely fills the distribution channel around its circumference. This permits creation of a back pressure in the melt which acts to break up or dissolve any existing gas bubbles within the melt before its reaching the filter pack. To create further back pressure, plus allow uniform melt flow substantially completely around the assembly, the channel gradually narrows in its longitudinal direction on each side of the melt point of entry from channel 12. At 14, which lies diametrically opposite this feed point, the width of the channel is zero.
As will be readily understood, it is possible to provide at least a portion of channel 13 in the adjoining wall of the housing; furthermore, it is possible to feed the melt into the distribution channel at a plurality of points, if desired.
Connecting along the entire lower circumference of distribution channel 13 is annular slot or circular space 15 which extends in downward direction between the housing 1 and inlet piece 2. As shown in FIGURE 1, annular space 15 is, over the greater part of its vertical length, defined by the outer circumference of filter pack 3. Filter pack 3 is made up of a series of superimposed filter gauzes or screens 16 which are in an alternating arrangement with metal plates 17. Thus, between every two successive plates is a filter through which the melt must flow in a horizontal direction which acts to further blend in or break up any existing gas bubbles which may exist in the polymer melt. The grooved downwardly extending inlet piece stem 18 fits into a central bore of filter pack 3 and is provided with four ribs 19 distributed over its circumference, serving to positively center filter elements 16 and plates 17. Grooves 20 between ribs 19 form channels through which the filtered melt flow to collecting space 24 and spinneret 5. The direction of melt flow is indicated by the arrows. A centering ring support member 21 is provided with a number of centering extensions 22 for inlet piece 2. Filter pack 3 is placed on stem 18 and enclosed between centering support 21 and a support plate 4. Support plate 4 extends around the end portion of the stem support ring 23 which is composed of an elastic material such as rubber and the like. Channels 20 open into space 24 between supporting plate 4 and spinneret plate 5. Numerals 25 represent the spinning orifices in the plate. FIGURE 2, a plan view along lines II-II of FIG- URE 1, shows the manner in which the polymer feed conduit 12 opens into the distribution channel.
FIGURE 3, a plan view along lines III-HI of'FIG- URE 1, shows the filter pack arrangement surrounding inlet piece. stem 18 and being positioned by ribs 19.
FIGURE 4 shows a slightly modified embodiment of the apparatus according to this invention. The lowermost end of annular space 15 is shaped in a manner to permit the melt to be fed to filter pack 3 along its entire circumference as 'well' as at the top. The filter pack in the embodiment is made up of a rather coarse-meshed filter screen 26, which is alternated with a finer mesh filter screen 27. The filter pack assembly is, in this assembly, like FIGURE 1, supported by plate 4, having the centrally disposed polymer fiow channel, 28. Plate 4 can be positioned directly on the spinneret plate (not shown). The filter pack is enclosed at its top by a circular plate 29, having a central opening and further having recesses 31 along its outer circumference. The melt flows through the filter pack both in vertical and horizontal direction (the direction of flow is indicated by the arrows), thus permitting a large, effective filtering surface for the melt. This permits the filter pack to be used for a longer period before it has to be replaced. The lower end inlet piece 2 is modified to permit the melt flowing l the filter pack both through recesses 31 and bore 30.
FIGURE 5 shows a cross-sectional view of an additional embodiment of the melt spinning apparatus according to this invention. Sealing against polymer leakage in this embodiment is elfected by the pressure of the molten polymer passing through the housing. Top or closure 32 is screwed into the housing 1. Between inlet piece 2 and closure 32 is a sealing ring or resilient gasket 34. By its movement within the housing, the inlet piece exerts pressure directly on gasket 34 as soon as the melt enters the assembly and pressures begin to build. The assembly of this embodiment is the top-loaded type, which means that the assembly is lowered into a fixedly mounted, heated jacket for a spinning operation. Assemblies of this configuration permit easy replacement, for instance, after being in service for several weeks, the assembly can be easily removed, using lifting eye 33, and replaced by a clean assembly. The main feed conduit for the melt is connected to opening 35 in the side of the housing in order to permit changing without completely shutting down the remaining chip melting and/ or polymerization apparatus. Opening 35 feeds directly into distribution channel 13, the width of which again decreases in the direction of the polymer flow. The melt flows from the distribution channel 13 downwardly through annular slot 15 defined by the arrangement of parts, in the direction indicated by the arrows. Beneath inlet piece 2 is filter pack 3, through which the melt flows perpendicular to the plane of the arrangement of filters.
FIGURE 5 further shows, on each side of the broken line, two slightly different constructions of the lower end of inlet piece 2. Left of the line shows an expedient wherein part of the polymer is guided by bafile means 36 from the wall of the housing to the center of the assembly and then is distributed over the filter. In the embodiment shown to the right of the line, the molten polymer flows from annular slot 15 directly to the filter. The filament arrangement and elements below are identical in both instances. Support plate 4. isprovided with a series of openings through which the polymer passes to spinneret die plate 5.
The invention in its broader aspects is not limited to the specific apparatus shown and described, but departures may be made therefrom within the scope of the accompanying claims Without departing from the prin-- feed conduitv for receiving a molten polymeric ma terial from apressurized source,
(0) said conduit directly communicating with a horizontally disposed distribution channel, a wall of which is formed by said plug downstream frorn-said feed conduit,
(d) said channel further communicating along substantially its entire length with the interior wall of said spinneret housing,
(e) a filter pack interposed between said distribution channel and a spinneret plate, and
(f) said spinneret plate having a plurality of shaping orifices arranged to receiveand shape the molten polymer into filaments.
2. Apparatus as defined in claim 1 in which the polymer melt distribution channel narrows in a longitudinal direction on each side of the point where said feed conduit communicates with said channel.
plug is provided with a plurality of spacing, members.
distributed along its circumference to center the plug With respect to the spinneret housing.
4. A spinneret pack assembly comprising a housing, an inlet piece within the housing having at least one feed conduit adapted to receive a molten polymeric material from a pressurized source and having a projecting stem projecting from the bottom thereof said stem having extending ribs for centering a plurality of filter screens disposed around said stem and a plurality of grooves between said ribs adapted to receive and guide the molten polymer to a spinneret plate.
5. Apparatus as defined in claim 1 in which the filter pack is composed of a plurality of alternating layers of screens having different mesh sizes.
6. Apparatus as defined in claim 1 in which the fill plug is adapted for movement Within the housing when under the influence of pressure.
References Cited UNITED STATES PATENTS FOREIGN PATENTS Canada. France. Germany.
WILLIAM J. STEPHENSON, Primary Examiner.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US1984472 *||7 May 1929||18 Dec 1934||Aceta Gmbh||Manufacture of artificial threads|
|US2560778 *||28 Feb 1950||17 Jul 1951||British Insulated Callenders||Extrusion apparatus for covering cores|
|US2784843 *||10 Aug 1954||12 Mar 1957||American Viscose Corp||Filter construction|
|US2869176 *||13 Aug 1951||20 Jan 1959||Du Pont||Spinneret pack|
|US2871511 *||24 Aug 1954||3 Feb 1959||Ici Ltd||Melt spinning apparatus|
|US2881474 *||26 Sep 1955||14 Apr 1959||American Cyanamid Co||Spinning device|
|CA524446A *||1 May 1956||American Cyanamid Co||Device for use in spinning viscous spinning solutions|
|DE1140337B *||7 Nov 1959||29 Nov 1962||Troester Maschf Paul||Spritzkopf fuer die Herstellung von Schlaeuchen, Schlauchfolien usw. aus thermoplastischen Werkstoffen|
|FR1210419A *||Title not available|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3436448 *||3 Feb 1966||1 Apr 1969||American Cyanamid Co||Method and apparatus for spinning uniform fibers|
|US3458900 *||24 Jul 1967||5 Aug 1969||Toray Industries||Spinning pack assembly for manufacturing composite filaments|
|US3500499 *||1 Jun 1967||17 Mar 1970||Inventa Ag||Spinning device for synthetic fibers|
|US3540080 *||21 Sep 1967||17 Nov 1970||Inventa Ag||Device for the spinning of multicomponent synthetic fibers|
|US4361489 *||17 Jun 1980||30 Nov 1982||Akzona, Incorporated||Device for filtering a liquid and a spinning assembly provided with such a filter|
|US5387097 *||7 Dec 1992||7 Feb 1995||Akzo Nv||Self-sealing spin pack|
|US5629080 *||13 Jan 1993||13 May 1997||Hercules Incorporated||Thermally bondable fiber for high strength non-woven fabrics|
|US5654088 *||6 Jun 1995||5 Aug 1997||Hercules Incorporated||Thermally bondable fiber for high strength non-woven fabrics|
|US5705119 *||7 Feb 1996||6 Jan 1998||Hercules Incorporated||Process of making skin-core high thermal bond strength fiber|
|US5733646 *||6 Jun 1995||31 Mar 1998||Hercules Incorporated||Thermally bondable fiber for high strength non-woven fabrics|
|US5882562 *||29 Dec 1997||16 Mar 1999||Fiberco, Inc.||Process for producing fibers for high strength non-woven materials|
|US5888438 *||13 Feb 1997||30 Mar 1999||Hercules Incorporated||Thermally bondable fiber for high strength non-woven fabrics|
|US6116883 *||7 Feb 1996||12 Sep 2000||Fiberco, Inc.||Melt spin system for producing skin-core high thermal bond strength fibers|
|US20080289665 *||1 Jul 2005||27 Nov 2008||Martin John Dwyer||Apparatus for Cleaning a Refuse Bin|
|CN100523333C||12 Apr 2007||5 Aug 2009||周光明||Network nozzle device with detachable cover plate|
|DE3024108A1 *||27 Jun 1980||4 Jun 1981||Barmag Barmer Maschf||Vorrichtung zum filtern einer fluessigkeit und spinnvorrichtung mit einem derartigen filter|
|DE19643425C2 *||22 Oct 1996||2 Dec 1999||Geb Schroeder Beeck||Sandlose Spinndüse|
|EP0545375A2 *||2 Dec 1992||9 Jun 1993||Akzo Nobel N.V.||Self-sealing spinneret pack|
|EP0545375A3 *||2 Dec 1992||8 Dec 1993||Akzo Nv||Self-sealing spinneret pack|
|International Classification||D01D4/08, D01D4/02, B29C47/68|
|Cooperative Classification||D01D4/08, B29C47/68, B01D25/04, B29C47/686, B29C47/0009|
|European Classification||B29C47/68, D01D4/08, B01D25/04|