US2990236A - Spinning process - Google Patents
Spinning process Download PDFInfo
- Publication number
- US2990236A US2990236A US722159A US72215958A US2990236A US 2990236 A US2990236 A US 2990236A US 722159 A US722159 A US 722159A US 72215958 A US72215958 A US 72215958A US 2990236 A US2990236 A US 2990236A
- Authority
- US
- United States
- Prior art keywords
- filaments
- guide
- spinneret
- guides
- spinning process
- 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.)
- Expired - Lifetime
Links
- 238000009987 spinning Methods 0.000 title description 7
- 239000000463 material Substances 0.000 claims description 10
- 238000002074 melt spinning Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 claims description 3
- 238000000034 method Methods 0.000 description 5
- 239000000919 ceramic Substances 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 239000011651 chromium Substances 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 235000004879 dioscorea Nutrition 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- -1 polyethylene terephthalate Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Images
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
- D01D5/08—Melt spinning methods
Definitions
- the bundle of extruded filaments may be collected by winding them, for example, onto surface driven bobbins.
- Filamentary material made in this way has been found to be irregular with respect both to the overall denier of the bundle and also the denier of individual filaments produced substantially at the same instant of time. It is well known that these variations seriously affect the quality of the textile materials made from the filamentary material.
- the object of my invention may be attained by ensuring that the filaments in passing around the guides are deflected through angles within the range of 5 to 90 we prefer that the angle of deflection should be within the range of 30 to 60 as this range provides the mininum denier variability consistent with threadline stability.
- the guide or guides comprise one or more low friction thread constraining surfaces.
- the yarn contacting surfaces of my guide may be of any suitable material and I have found that guides made from ceramics with surfaces of low coeflicient of friction and sand blasted matt-chromium plated metal are particularly satisfactory.
- the guides of my invention may be of tubular construction and adapted to be cooled internally.
- the guides may be fixed or capable of rotation by the moving filaments. I have found that light weight freely rotatable rollers are suitable and if fine circumferential grooves are cut around the roller the individual filaments Harrogate,'England, assignor to perial Chemical Industries Limited, London, England,
- FIGURE 4 shows the use of a plain idler roller as a deflecting guide and FIGURE 5 illustrates a grooved idler roll.
- extruded filaments 1 from a spinneret 2 pass individually through a number of guides 3 which are substantially equally spaced about the periphery of a rigid guide ring 4 to a convergence yarn guide 5 and to a wind up means 6 (schematically shown).
- the guide ring 4 is arranged beneath the spinneret 2 in the region Where the filaments solidify and become non-tacky and the diameter of the guide ring is such that each filament is deflected through an angle (FIGURE 2) where 0 is greater than 5 and less than In FIGURE 4 the filaments are deflected around a free running idler roll 7, A" in diameter, mounted in a support 8.
- the idler roll may be conveniently made of sand blasted steel with a chromium plated skin.
- FIGURE 5 illustrates a preferred type of free running idler roll 9 provided with fine circumferential grooves 10.
- Table 1 illustrates the percentage coeflicient of variation of yarns comprising 48 filaments of polyethylene terephthalate of 1 and 2 denier per filament (drawn) when passed around an Alsimag (registered trademark) ceramic guide located so as to deflect the yarns through a range of angles of 0 to 60.
- the vertical distance below the spinneret for the 1 denier per filament yarn was 19 inches and for the 2 denier per filament yarn 26".
- Both yams were spun through 48 hole spinnerets, the spinning temperature was 290 C. and the wind-up speed 3000 ft./min.
- the denier per filament was altered by adjusting the speed of the gear pump.
- substantially equal fractions of a number of filaments coming from the spinneret each pass around a separate guide, said separate guides being equally spaced around the periphery of a rigid ring located between the spinneret and the wind-up means. I have found it preferable that the fraction of a number offilaments is not greater than one quarter.
- a melt spinning process for the production of fine denier filaments comprising extruding molten polymer through a multi-hole spinneret to form filaments, and passing the resultant filaments without material frictional drag about guide means located in the region where the filaments solidify and become substantially non-tacky to Patented June 27, 1961 moons-e
- a i 3 a wind-up means, characterized in that the filaments in passing around the guide means are deflected through an angle of not, less than 5" and not more than 90.
- the guide means comprisesat, least one light weight freely rotabl'e roller.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Textile Engineering (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Preliminary Treatment Of Fibers (AREA)
Description
June 27, 1961 E. l. RISELEY 2,990,236
SPINNING PROCESS Filed March 18, 1958 2 Sheets-Sheet 1 I Ema fmw F/SH EV ATTORNEYS June 27, 1961 1, RISELEY 2,990,236
SPINNING PROCESS Filed March 18, 1958 \I I l\\\\\\\\\\\\\\\\\\ 2 Sheets-Sheet 2 n 'JENTOR Z/wc [m/v 65.45 y
ww mm ATTORNEYS Un ed Se ee *9" 2,990,236 p I S INNINGPROCE-SS Eric 'IvanRisel'ey,
a corporation of Great Britain v Filed Mar.'18, '1958, Ser. No.722,1-59 1 Claims p1iority,'application Great Britain 25, 1957 V i 5 Claims. (Cl. 18-54) This invention relates to an improved melt spinning process.
In themelt'spinning of high polymers to producefine filamentary "materials-of lessthan '3 denier per filament by extrusion through multi-holed spinnerets, the bundle of extruded filaments may be collected by winding them, for example, onto surface driven bobbins. Filamentary material made in this way has been found to be irregular with respect both to the overall denier of the bundle and also the denier of individual filaments produced substantially at the same instant of time. It is well known that these variations seriously affect the quality of the textile materials made from the filamentary material.
Certain of these denier variations cannot be attributed to such mechanical causes as the traverse mechanism and the winding-up unit and are therefore not easily overcome and so far they have defied attempts at correction. These variations are irregular in amplitude.
It is well known that as the extruded fine filaments leave the spinneret they cool down and eventually harden at a distance some inches below the spinneret face. In British patent specification No. 661,999 there is disclosed a process of spinning fine denier filament yarns from a melt of synthetic filament forming polymeric materials wherein a melt of said polymeric materials is extruded through a multi-hole spinneret into a stream of inert gas passing through a spinning cell and maintained at a temperature suflicient to cool said molten polymeric material to below its solidification temperature whereby to form simultaneously a plurality of fine denier filaments with the improvement which comprises collecting said filaments into a yarn and steadying said yarn as soon as said filaments solidify and become substantially non-tacky by means of convergence yarn guide.
According to my invention I provide an improvement in the process of British Patent No. 661,999 wherein the filaments after leaving the spinneret pass, under tension, over one or more guides located between the spinneret and the wind up means, the guide or guides being in the region wherein the filaments solidify and become substantially non-tacky, characterised in that the filaments in passing round the guide or guides are deflected through an angle of not less than 5 and not greater than 90.
Whilst the object of my invention may be attained by ensuring that the filaments in passing around the guides are deflected through angles within the range of 5 to 90 we prefer that the angle of deflection should be within the range of 30 to 60 as this range provides the mininum denier variability consistent with threadline stability.
Preferably the guide or guides comprise one or more low friction thread constraining surfaces. The yarn contacting surfaces of my guide may be of any suitable material and I have found that guides made from ceramics with surfaces of low coeflicient of friction and sand blasted matt-chromium plated metal are particularly satisfactory.
The guides of my invention may be of tubular construction and adapted to be cooled internally.
The guides may be fixed or capable of rotation by the moving filaments. I have found that light weight freely rotatable rollers are suitable and if fine circumferential grooves are cut around the roller the individual filaments Harrogate,'England, assignor to perial Chemical Industries Limited, London, England,
are, separated as they pass over the roller and are there oi g'uides'insuch a position that the birefringence of thefilament leaving the guidesis increased by about 20%- over the birefringence value obtained when the guide or guides are removed.
The attached drawings illustrate but do not linut the scope of my invention FIGU-RES l and. 2'are side elevations of a rigid guide ring and-FIGURE 3 a plan viewof said'ring.
FIGURE 4 shows the use of a plain idler roller as a deflecting guide and FIGURE 5 illustrates a grooved idler roll.
With reference to FIGURES 1, 2, and 3, extruded filaments 1 from a spinneret 2 pass individually through a number of guides 3 which are substantially equally spaced about the periphery of a rigid guide ring 4 to a convergence yarn guide 5 and to a wind up means 6 (schematically shown).
The guide ring 4 is arranged beneath the spinneret 2 in the region Where the filaments solidify and become non-tacky and the diameter of the guide ring is such that each filament is deflected through an angle (FIGURE 2) where 0 is greater than 5 and less than In FIGURE 4 the filaments are deflected around a free running idler roll 7, A" in diameter, mounted in a support 8. The idler roll may be conveniently made of sand blasted steel with a chromium plated skin.
FIGURE 5 illustrates a preferred type of free running idler roll 9 provided with fine circumferential grooves 10.
Table 1 illustrates the percentage coeflicient of variation of yarns comprising 48 filaments of polyethylene terephthalate of 1 and 2 denier per filament (drawn) when passed around an Alsimag (registered trademark) ceramic guide located so as to deflect the yarns through a range of angles of 0 to 60. The vertical distance below the spinneret for the 1 denier per filament yarn was 19 inches and for the 2 denier per filament yarn 26". Both yams were spun through 48 hole spinnerets, the spinning temperature was 290 C. and the wind-up speed 3000 ft./min. The denier per filament was altered by adjusting the speed of the gear pump.
In one version of my invention substantially equal fractions of a number of filaments coming from the spinneret each pass around a separate guide, said separate guides being equally spaced around the periphery of a rigid ring located between the spinneret and the wind-up means. I have found it preferable that the fraction of a number offilaments is not greater than one quarter.
What I claim is:
1. A melt spinning process for the production of fine denier filaments comprising extruding molten polymer through a multi-hole spinneret to form filaments, and passing the resultant filaments without material frictional drag about guide means located in the region where the filaments solidify and become substantially non-tacky to Patented June 27, 1961 moons-e A i 3 a wind-up means, characterized in that the filaments in passing around the guide means are deflected through an angle of not, less than 5" and not more than 90.
2. A process according to claim 1, wherein the fila-' ments are deflected through an angle not. less than 30" and not more than 60.
3'. A process, according to claim 2, wherein the guide means comprisesat, least one light weight freely rotabl'e roller.
4.. A process according to claim 3, wherein fine circum ferential grooves are cut into the surface of the roller in planes at. right angles to the axis of the roller.
5. In a melt spinning process for the production of fine ing the filaments fromthe spinneret without material frictional drag about the periphery of a guide ring located in the region where the filaments solidify and become substantially non-tacky, thereby deflecting each of the filaments through an angleof not, less than and not more than, and conducting the filaments to a wind-up References Cited in theme of this: patent UNITED STATES PATEN'IIS- 1,951,181 Battin Mar. 13, 1934 2',595,044 Zmatlik et a1. Apr. 29, 1952 2,624,934 Munson et al. Jan. 13 195.3,- 2,76Z,429 McCrosky Oct. 23, 1956 Sharp Sept. 16, 8
Claims (1)
1. A MELT SPINNING PROCESS FOR THE PRODUCTION OF FINE DENIER FILAMENTS COMPRISING EXTRUDING MOLTEN POLYMER THROUGH A MULTI-HOLE SPINNERET TO FORM FILAMENTS, AND PASSING THE RESULTANT FILAMENTS WITHOUT MATERIAL FRICTIONAL DRAG ABOUT GUIDE MEANS LOCATED IN THE REGION WHERE THE FILAMENTS SOLIDIFY AND BECOME SUBSTANTIALLY NON-TACKY TO
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9715/57A GB833032A (en) | 1957-03-25 | 1957-03-25 | Process for melt spinning synthetic filaments |
Publications (1)
Publication Number | Publication Date |
---|---|
US2990236A true US2990236A (en) | 1961-06-27 |
Family
ID=9877377
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US722159A Expired - Lifetime US2990236A (en) | 1957-03-25 | 1958-03-18 | Spinning process |
Country Status (4)
Country | Link |
---|---|
US (1) | US2990236A (en) |
BE (1) | BE566016A (en) |
FR (1) | FR1193580A (en) |
GB (1) | GB833032A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3065614A (en) * | 1960-05-03 | 1962-11-27 | Johns Manville | Apparatus for attenuating glass fibers |
US3107972A (en) * | 1962-10-24 | 1963-10-22 | Du Pont | Process for producing bulkable filamentary polyamide yarns |
US3271825A (en) * | 1963-10-03 | 1966-09-13 | Fiberglas Canada Ltd | Method of conditioning glass fiber strands |
US3511905A (en) * | 1967-08-22 | 1970-05-12 | Viscose Suisse Soc | Process for the preparation of synthetic polymer filaments |
US3832435A (en) * | 1970-07-03 | 1974-08-27 | Hoechst Ag | Process for the manufacture of crimped fibers and filaments of linear high molecular weight polymers |
US3923224A (en) * | 1972-05-26 | 1975-12-02 | Ici Ltd | Filament handling apparatus |
US4000238A (en) * | 1972-02-29 | 1976-12-28 | Fiber Industries, Inc. | Method for production of synthetic yarns |
US4038357A (en) * | 1972-06-28 | 1977-07-26 | Imperial Chemical Industries Inc. | Manufacture of synthetic filaments |
CN103993372A (en) * | 2014-05-26 | 2014-08-20 | 苏州东茂纺织实业有限公司 | Pile generation device |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3091805A (en) * | 1960-11-02 | 1963-06-04 | Du Pont | Apparatus and process for drawing yarn |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1951181A (en) * | 1930-08-09 | 1934-03-13 | Revere Rubber Co | Method and apparatus for separating the individual strands of a rope |
US2595044A (en) * | 1948-06-01 | 1952-04-29 | Elite Sdruzene Tovarny Puncoch | Device for drawing off artificial fibers from the spinneret, especially fibers spun from the molten mass |
US2624934A (en) * | 1948-04-23 | 1953-01-13 | W M Steele Company Inc | Method of and apparatus for heat treatment of filamentary material |
US2767429A (en) * | 1952-05-06 | 1956-10-23 | Du Pont | Snubbing pin for drawing yarn |
US2851732A (en) * | 1953-07-14 | 1958-09-16 | Du Pont | Split filament bundle at finish roll |
-
0
- BE BE566016D patent/BE566016A/xx unknown
-
1957
- 1957-03-25 GB GB9715/57A patent/GB833032A/en not_active Expired
-
1958
- 1958-03-18 US US722159A patent/US2990236A/en not_active Expired - Lifetime
- 1958-03-25 FR FR1193580D patent/FR1193580A/en not_active Expired
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1951181A (en) * | 1930-08-09 | 1934-03-13 | Revere Rubber Co | Method and apparatus for separating the individual strands of a rope |
US2624934A (en) * | 1948-04-23 | 1953-01-13 | W M Steele Company Inc | Method of and apparatus for heat treatment of filamentary material |
US2595044A (en) * | 1948-06-01 | 1952-04-29 | Elite Sdruzene Tovarny Puncoch | Device for drawing off artificial fibers from the spinneret, especially fibers spun from the molten mass |
US2767429A (en) * | 1952-05-06 | 1956-10-23 | Du Pont | Snubbing pin for drawing yarn |
US2851732A (en) * | 1953-07-14 | 1958-09-16 | Du Pont | Split filament bundle at finish roll |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3065614A (en) * | 1960-05-03 | 1962-11-27 | Johns Manville | Apparatus for attenuating glass fibers |
US3107972A (en) * | 1962-10-24 | 1963-10-22 | Du Pont | Process for producing bulkable filamentary polyamide yarns |
US3271825A (en) * | 1963-10-03 | 1966-09-13 | Fiberglas Canada Ltd | Method of conditioning glass fiber strands |
US3511905A (en) * | 1967-08-22 | 1970-05-12 | Viscose Suisse Soc | Process for the preparation of synthetic polymer filaments |
US3832435A (en) * | 1970-07-03 | 1974-08-27 | Hoechst Ag | Process for the manufacture of crimped fibers and filaments of linear high molecular weight polymers |
US4000238A (en) * | 1972-02-29 | 1976-12-28 | Fiber Industries, Inc. | Method for production of synthetic yarns |
US3923224A (en) * | 1972-05-26 | 1975-12-02 | Ici Ltd | Filament handling apparatus |
US4038357A (en) * | 1972-06-28 | 1977-07-26 | Imperial Chemical Industries Inc. | Manufacture of synthetic filaments |
CN103993372A (en) * | 2014-05-26 | 2014-08-20 | 苏州东茂纺织实业有限公司 | Pile generation device |
Also Published As
Publication number | Publication date |
---|---|
FR1193580A (en) | 1959-11-03 |
BE566016A (en) | |
GB833032A (en) | 1960-04-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2990236A (en) | Spinning process | |
US3299469A (en) | Melt-spinning apparatus | |
FI94777C (en) | Method and apparatus for making composite yarn | |
US4069566A (en) | Take-up method of continuous filament bundles of synthetic fibers and apparatus therefor | |
GB1243668A (en) | An improved process and apparatus for the manufacture of fibrillary products, and products thus obtained | |
RU2276209C2 (en) | Method and apparatus for producing of composite thread | |
GB1344394A (en) | Apparatus for manufacturing filaments from molten synthetic material | |
US3061874A (en) | Melt spinning apparatus | |
US3083522A (en) | Production of textile yarns | |
US3777470A (en) | Method of forming a yarn package | |
US2932850A (en) | Production of filaments of uneven denier | |
JPS5822565B2 (en) | High speed spinning method | |
US3996324A (en) | Process for producing oriented continuous yarns | |
US3342027A (en) | Coalesced multifilament yarn | |
US3763521A (en) | Manufacture of non-woven materials | |
US2946526A (en) | Continuous method for winding up yarns | |
US3279711A (en) | Winding apparatus for melt-spun or dry-spun filaments | |
US3720382A (en) | Process and apparatus for the continuous production of synthetic threads | |
US2366278A (en) | Spinning process | |
KR100314561B1 (en) | Godet roller for dry type spinning device and dry type spinning method using the same | |
US2001000A (en) | Production of artificial filaments, yarns, or threads | |
US3470583A (en) | False twisting | |
US3353210A (en) | Rectangular convergence guide | |
US3466864A (en) | Twisting fibrous strands | |
US2083252A (en) | Method of producing artificial thread |