US2908937A - Method and apparatus for the manufacture of yarn - Google Patents
Method and apparatus for the manufacture of yarn Download PDFInfo
- Publication number
- US2908937A US2908937A US556256A US55625655A US2908937A US 2908937 A US2908937 A US 2908937A US 556256 A US556256 A US 556256A US 55625655 A US55625655 A US 55625655A US 2908937 A US2908937 A US 2908937A
- Authority
- US
- United States
- Prior art keywords
- yarn
- tube
- spinneret
- liquid
- section
- 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
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 238000000034 method Methods 0.000 title description 10
- 238000009987 spinning Methods 0.000 claims description 20
- 238000001125 extrusion Methods 0.000 claims description 6
- 230000001112 coagulating effect Effects 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 description 31
- 229920000297 Rayon Polymers 0.000 description 13
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 4
- 230000015271 coagulation Effects 0.000 description 4
- 238000005345 coagulation Methods 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- 239000002964 rayon Substances 0.000 description 3
- 239000001117 sulphuric acid Substances 0.000 description 3
- 235000011149 sulphuric acid Nutrition 0.000 description 3
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 230000001627 detrimental effect Effects 0.000 description 2
- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- JUWSSMXCCAMYGX-UHFFFAOYSA-N gold platinum Chemical compound [Pt].[Au] JUWSSMXCCAMYGX-UHFFFAOYSA-N 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000012991 xanthate Substances 0.000 description 1
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 1
- 235000009529 zinc sulphate Nutrition 0.000 description 1
- 239000011686 zinc sulphate Substances 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
- D01D5/06—Wet spinning methods
Definitions
- the liquid in this portion is greater than the velocity in the second tube portion.
- the velocity in the first portion varies in direct relation to the ratio between yarn by means of the liquid portion of the spinning zone where tenacity, high denier, viscose the cross-sections .of the surfaces .of both'tube portions. It can be seenfrom this that the velocity of the liquid in .the first tube portion can be increased to the extent necessary and is most efiicient at substantially the velocity of the yarn. In this way, the yarn passes in a straight line, but under a minimum of tension, until it has been sufiiciently coagulated and regenerated to apply more tension. i 4
- a hook or other manual device can be used, but preferably a liquid head can be temporarily maintained so that the yarn is propelledby hydrostatic pressure of thec'haracter such as that shown in co-pending application Serial No. 515,146, filed June 13, 1955, now Patent No. 2,834,046 which is assigned to the same assignee as the present application.
- the figure which shows a preferred embodiment of the invention, is a diagrammatic view in elevation of the spinneret, tube and spinbath'assembly.
- a spinneret 10 mounted on a supply tube 11 which is connected to a viscose conduit, not shown, The spinneret 10 is submerged in a sulphuric acid containing spinbath 12.
- a twodiameter tube 13 is mounted in supports l4 and 15 and disposed concentrically with respect to spinneret 10. As shown, the tube 13 consists of a smaller diameter section 16, a middle frusto-conical section 17, a larger diameter section 18, and is open at bothends.
- The'srnaller section 16 of the tube is provided with a flanged inlet end 19 adjacent the spinneret 10,, and is in the shape of a fiat trumpet.
- the yarn 20 is formed of a plurality of filaments as it is drawn through the orifices in the face of 'spinneret 10, and is guided by means of roller 21 which is disposed adjacent the outlet end of the'larger, section 18 of tube 13.
- the yarn is 'then drawn from the bath by any suitable means, such as a godet, not shown, located beyond guide roller 22; or the guide roller 22 can be positively driven for propelling the yarn.
- the process is particularly adapted for spinning high yarn which has been prepared by adding to the viscose or the spinbath, or both, some of thewell-known regenerationretardants such as quinoline, hexamethylenediamine, mono-isopropanol, etc.
- some of thewell-known regenerationretardants such as quinoline, hexamethylenediamine, mono-isopropanol, etc.
- the yarn that is formed is extremely sensitive to exterior influences near the spinneret. Therefore, by using a tube of such shape that the yarn per se can regulate the velocity of the liquid in the first part of the coagulating zone, an extremely eflicient treatment of the yarn at high speeds can be realized.
- the yarn can be collected at substantially higher speeds and with high stretching without any detrimental effects resulting.
- each portion of the tube depends on the denier of the yarn to bespun and the size of the spinnerets employed. In each case, it is a simple matter for one'skilled in the art to select the effective cross-section that corresponds with the inner diameter of the smaller tubeportion, namely, it should only slightly exceed the outer ring of spinneret orifices. (See the figure.) Then it iseasy to select the proper cross-section and length of the second larger tube portion in such a way that the 3 coagulation liquid in the first tube portion moves at substantially the same velocity as the yarn, which prevents the liquid from exercising any detrimental mechanical action on the yarn.
- the frusto-conical portion connects the smaller and larger sections at a gradual taper, 7
- the inner diameter of the smaller portion of the spinning tube is preferably 20-40% larger than that of the outer ring of the spinneret orifices.
- the inlet opening is in the shape of a short flat trumpet and is disposed concentrically as close as possible 1 to the spinneret.
- it is preferable to gradually taper the frusto-conical portion whereby the sucking action obtains a maximum value and the filaments of the yarn spread uniformly throughout the interior of the tube.
- the outer ring of spinneret orifices has, for example, a diameter of about 9 mm., in which case the smaller tube portion should be about 10-12 mm.
- the inner diameter of the wide tube portion should be about 1.2 to 1.5 times larger than the narrow tube portion. It has been determined that the length of the wide tube portion should be 25-40 cm. in order to exercise a satisfactory sucking action. With respect to the middle frustoconical portion, it has been found that its length should, at most, be twice that of the inner diameter of the wide tube portion.
- the improvement which comprises a spinning tube mounted concentric with the spinneret, said spinning tube having two cylindrical tube sections of different diameters connected intermediate the ends thereof by a frusto-conical section, the smaller tube section being slightly larger than the diameter of the example, 1600 denier, for use in making tire cord, the I diameter of the outer ring of spinneret orifices is usually about 16 mm., in which case, the inner diameter of the narrow tube portion should be approximately 20-22 mm.
- a tube may be satisfactory which has a narrow tube portion length of 30 cm., and a diameter of 21 mm.
- the second portion has a length of 20 cm. and a diameter of 27 mm.
- the frusto-conical portion has a length of 5 cm.
- the inlet opening of the narrow tube portion is preferably provided with a flat trumpet-shaped flange, and is placed as close as possible to the spinneret face without inhibiting the free flow of coagulation liquid into the tube or causing a turbulence.
- the correct spacing is determined by the denier of the yarn, the diameter of the spinneret face, and the spinning velocity. As a rule it is preferred to space the inlet opening a distance of 5-20 mm. from the face of the spinneret.
- Example A viscose solution was prepared from cotton linters having a cellulose content of 7.7% by weight, an alkali content of 5.5% by weight, a xanthate ratio of 0.47 and a ball fall viscosity of 60 sec., to which 0.16% by weight of quinoline was added. It was spun, by means of the system described above, in a spinbath maintained at 60 C. containing 6% by weight of sulphuric acid, 19% by weight of sodium sulphate and 3.8% by weight of zinc sulphate. In the spinning operation a gold-platinum spinneret was used in which 1060 orifices each having a diameter of 60 micron had been drilled.
- the diameter of the outer ring of spinning orifices was 16 mm..
- the narrower tube portion had an inner diameter of 21 mm., the wider tube portion an inner diameter of 27 mm., the length of the narrow tube portion being 30 cm. and that of the wider tube portion 19 cm.
- the length of the frustoconical portionbetween these two portions was 4 cm. long.
- the outer diameter of the trumpet-shaped inlet opening was 4 cm. This inlet opening was situated at a distance of 2 cm. from the spinneret.
- the primary drawing-01f speed was m./min. and the winding-up speed was 80 m./min., the resulting stretch being 100%.
- apparatus for the manufacture of rayon including a spinneret to extrude a spinning solution into an acid coagulating bath to form yarn therefrom and means to withdraw the yarn from the bath at a higher velocity than the rate of extrusion
- the improvement which comprises a spinning tube mounted concentrically 5-20 mm. from the face of the spinneret, said tube consisting of two cylindrical sections of different diameters connected by a gradually tapering section intermediate the ends of said spinning tube, the inlet end of the smaller tube section being nearer the spinneret than the larger tube section and the inner diameter of the larger tube section being 1.21.5 times greater than the inner diameter of the smaller tube section.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Textile Engineering (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Artificial Filaments (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL337977X | 1955-01-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
US2908937A true US2908937A (en) | 1959-10-20 |
Family
ID=19784602
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US556256A Expired - Lifetime US2908937A (en) | 1955-01-11 | 1955-12-29 | Method and apparatus for the manufacture of yarn |
Country Status (7)
Country | Link |
---|---|
US (1) | US2908937A (enrdf_load_stackoverflow) |
BE (2) | BE550120A (enrdf_load_stackoverflow) |
CH (2) | CH337977A (enrdf_load_stackoverflow) |
DE (2) | DE1112604B (enrdf_load_stackoverflow) |
FR (2) | FR1144219A (enrdf_load_stackoverflow) |
GB (2) | GB784896A (enrdf_load_stackoverflow) |
NL (1) | NL84656C (enrdf_load_stackoverflow) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3071806A (en) * | 1958-01-29 | 1963-01-08 | Celanese Corp | Wet spinning column and process |
US4159299A (en) * | 1976-04-06 | 1979-06-26 | Serkov Arkady T | Method for the production of rayon |
US20080023873A1 (en) * | 2004-09-17 | 2008-01-31 | Birla Research Institute For Applied Sciences | Process for Preparing a Non-Woven Cellulosic Structure and the Non-Woven Cellulosic Structure Prepared Therefrom |
US20130300013A1 (en) * | 2008-04-18 | 2013-11-14 | Mitsubishi Rayon Co., Ltd. | Wet spinning apparatus and method for wet spinning |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL244855A (enrdf_load_stackoverflow) * | 1958-11-21 | |||
DE3125221C2 (de) * | 1981-06-26 | 1987-05-07 | Ivan Gavrilovič Šimko | Verfahren zur Herstellung eines texturierten Hydratcellulosefadens und Vorrichtung zum Erzeugen eines Spinnkörpers |
RU2541284C1 (ru) | 2011-06-15 | 2015-02-10 | Трютцшлер Нонвоувенз Гмбх | Корыто прядильной ванны |
DE202013101041U1 (de) | 2013-03-11 | 2013-03-18 | TRüTZSCHLER GMBH & CO. KG | Vorrichtung zum Zuführen von Spinnmasse zu einer Spinndüse |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2243116A (en) * | 1936-03-09 | 1941-05-27 | American Bemberg Corp | Apparatus for use in manufacturing artificial filaments |
US2511699A (en) * | 1947-11-10 | 1950-06-13 | Comptoir Textiles Artificiels | Method for spinning viscose |
FR1026847A (fr) * | 1950-09-08 | 1953-05-05 | Procédé de fabrication de produits filés artificiels | |
US2642333A (en) * | 1949-07-26 | 1953-06-16 | Omni Products Corp | Method of spinning polyvinyl alcohol fibers |
US2659102A (en) * | 1951-03-14 | 1953-11-17 | Du Pont | Spinning viscose rayon |
US2700794A (en) * | 1950-07-31 | 1955-02-01 | British Celanese | Wet-spinning cells |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE478928C (de) * | 1929-07-04 | Fritz Tschirch Dr Ing | Spinnvorrichtung fuer das Streckspinnverfahren mit einem einen ringfoermigen Einlauffuer die Faellfluessigkeit bildenden, die Spinnbrause und den Trichter aufnehmenden Spinnkopf | |
DE644786C (de) * | 1937-05-13 | Fr Kuettner Akt Ges | Spinntrichter zur Herstellung von Kunstseide nach dem Streckspinnverfahren | |
DE509294C (de) * | 1930-10-06 | Fr Kuettner Akt Ges | Spinntrichter zur Herstellung von Kunstseide nach dem Streckspinnverfahren | |
US827434A (en) * | 1905-08-22 | 1906-07-31 | Ernst Willy Friedrich | Apparatus for the production of artificial threads. |
DE220051C (enrdf_load_stackoverflow) * | 1907-05-15 | |||
DE464384C (de) * | 1926-04-04 | 1928-08-16 | Karl Koske | Vorrichtung zum Spinnen von Kunstfaeden nach dem Streckspinnverfahren |
DE685803C (de) * | 1935-11-26 | 1939-12-27 | Eduard Wurtz | Vorrichtung zur Herstellung von Faeden aus Spinnloesungen, insbesondere von Kunstseidefaeden |
DE678210C (de) * | 1936-03-09 | 1939-07-10 | Bemberg Ag | Vorrichtung zum Herstellen von Kunstseide |
GB504132A (en) * | 1937-10-25 | 1939-04-20 | Courtaulds Ltd | Improvements in and relating to the manufacture and production of artificial threads |
US2386411A (en) * | 1943-04-17 | 1945-10-09 | American Viscose Corp | Device for collecting filamentary materials |
US2402846A (en) * | 1943-06-19 | 1946-06-25 | Albert O Ryan | Method of and means for forming filamentary articles |
US2550808A (en) * | 1949-10-25 | 1951-05-01 | Du Pont | Coagulating bath circulating eductor |
AT179606B (de) * | 1951-07-06 | 1954-09-25 | Onderzoekings Inst Res | Flüssigkeitsbehandlungswanne für laufende Fäden |
-
0
- NL NL84656D patent/NL84656C/xx active
- BE BE542542D patent/BE542542A/xx unknown
- BE BE550120D patent/BE550120A/xx unknown
-
1955
- 1955-11-04 CH CH337977D patent/CH337977A/de unknown
- 1955-11-04 DE DEA23723A patent/DE1112604B/de active Pending
- 1955-11-07 GB GB31819/55A patent/GB784896A/en not_active Expired
- 1955-12-05 FR FR1144219D patent/FR1144219A/fr not_active Expired
- 1955-12-29 US US556256A patent/US2908937A/en not_active Expired - Lifetime
-
1956
- 1956-08-02 DE DEA25424A patent/DE1123795B/de active Pending
- 1956-08-03 GB GB24022/56A patent/GB816687A/en not_active Expired
- 1956-08-03 CH CH341597D patent/CH341597A/de unknown
- 1956-08-09 FR FR70444D patent/FR70444E/fr not_active Expired
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2243116A (en) * | 1936-03-09 | 1941-05-27 | American Bemberg Corp | Apparatus for use in manufacturing artificial filaments |
US2511699A (en) * | 1947-11-10 | 1950-06-13 | Comptoir Textiles Artificiels | Method for spinning viscose |
US2642333A (en) * | 1949-07-26 | 1953-06-16 | Omni Products Corp | Method of spinning polyvinyl alcohol fibers |
US2700794A (en) * | 1950-07-31 | 1955-02-01 | British Celanese | Wet-spinning cells |
FR1026847A (fr) * | 1950-09-08 | 1953-05-05 | Procédé de fabrication de produits filés artificiels | |
US2659102A (en) * | 1951-03-14 | 1953-11-17 | Du Pont | Spinning viscose rayon |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3071806A (en) * | 1958-01-29 | 1963-01-08 | Celanese Corp | Wet spinning column and process |
US4159299A (en) * | 1976-04-06 | 1979-06-26 | Serkov Arkady T | Method for the production of rayon |
US20080023873A1 (en) * | 2004-09-17 | 2008-01-31 | Birla Research Institute For Applied Sciences | Process for Preparing a Non-Woven Cellulosic Structure and the Non-Woven Cellulosic Structure Prepared Therefrom |
US20130300013A1 (en) * | 2008-04-18 | 2013-11-14 | Mitsubishi Rayon Co., Ltd. | Wet spinning apparatus and method for wet spinning |
US9234301B2 (en) * | 2008-04-18 | 2016-01-12 | Mitsubishi Rayon Co., Ltd. | Method for wet spinning |
Also Published As
Publication number | Publication date |
---|---|
NL84656C (enrdf_load_stackoverflow) | |
BE550120A (enrdf_load_stackoverflow) | |
BE542542A (enrdf_load_stackoverflow) | |
CH337977A (de) | 1959-04-30 |
GB784896A (en) | 1957-10-16 |
DE1123795B (de) | 1962-02-15 |
FR1144219A (fr) | 1957-10-10 |
CH341597A (de) | 1959-10-15 |
FR70444E (fr) | 1959-05-06 |
GB816687A (en) | 1959-07-15 |
DE1112604B (de) | 1961-08-10 |
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