GB1088240A - Melt spinning of fibre-forming polymers - Google Patents
Melt spinning of fibre-forming polymersInfo
- Publication number
- GB1088240A GB1088240A GB35785/65A GB3578565A GB1088240A GB 1088240 A GB1088240 A GB 1088240A GB 35785/65 A GB35785/65 A GB 35785/65A GB 3578565 A GB3578565 A GB 3578565A GB 1088240 A GB1088240 A GB 1088240A
- Authority
- GB
- United Kingdom
- Prior art keywords
- polymer
- stream
- control surfaces
- streams
- flow
- 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
Links
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
- D01D5/088—Cooling filaments, threads or the like, leaving the spinnerettes
- D01D5/092—Cooling filaments, threads or the like, leaving the spinnerettes in shafts or chimneys
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Textile Engineering (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
1,088,240. Melt-spinning apparatus. IMPERIAL CHEMICAL INDUSTRIES Ltd. Aug. 2, 1966 [Aug. 20, 1965], No. 35785/65. Heading B5B. An apparatus for controlling the flow of ambient fluid in the vicinity of filaments while being melt-spun consists of deflecting means disposed at intervals along the lengths of the path of the stream or streams of polymer whereby the flow of the ambient fluid towards the stream or each stream of polymer and thereafter following a path of the, or of each, stream of polymer is a stable laminar flow, the said conditions of stable laminar flow persisting until the temperature of the, or of each, stream of polymer falls to the solidification point. Suitably, at least two control surfaces are arranged about the stream or streams of polymer in the form of a collar or forming in effect a collar, the inner edge of each of said control surfaces being distant by not less than about 4 mm. and not more than about 30 mm. from the stream of polymer or the outermost streams of polymer and the said control surface extending outwards to at least about 10 mm. from its inner edge, said control surfaces being distant from adjacent control surfaces by at least about 5 mm. and at most about 100 mm. and a point moving radially along a surface from the inner to the outer edge of each of said control surfaces having at no time any downward component of motion, adjacent control surfaces being optionally bridged by substantially vertically disposed laminae. Such collars may advantageously be in the form of the surface of a conical frustum with the wider part uppermost, or of the surface generated by the rotation of a portion of an exponential curve about the abscissa. Alternatively, the plurality of control surfaces may comprise a single member, e.g. a suitably offset Archimedean screw with at least two complete turns. As in Fig. 1, a series of six identical members 5, each consisting of a portion 6 in the form of the curved surface of a right conical frustum of conical angle 140 degrees, base 7 cm. diameter and top 1À75 cm. diameter, integral with an annular disc 11 of outside diameter 10 cm. and internal diameter 7 cm., are held in fixed juxtaposition, with the annular discs 11 being in parallel planes and the bases of the conical frustral portions 6 facing all in the same direction, by means of rods 7, 8 and 9 which are threaded and passed through holes of which there are three equid.stant bores through each annular disc 11 with centres 0.5 cm. from the outer edge of the disc 11. The members are held in their relative positions by means of nuts 10 screwed on the threaded rods 7, 8 and 9. The apparatus may be used not only with an array of spinneret holes with radial symmetry but also with other configurations, e.g. a rectangular configuration. In a modification, the top of the conical frustum was of 5-8 cm. diameter for the uppermost member reducing by uniform stages to 5.2 cm. for the lowermost member, this variation being in conformity with the convergence of the filaments to a guide 1-5 m. below the spinneret. A cylinder of gauze may be fitted around the assembly of members if desired, so that the induced flow of ambient air has to flow through the meshes of the gauze. A further improvement in the stability of the air can be effected by incorporating vertical fins in the space between adjacent control surfaces. The effect of the apparatus in inducing a laminar flow of ambient fluid towards the polymer streams and thereafter along with the polymer streams is such that the rate of heat transfer from the polymer streams to the ambient fluid is minimized. Thus for a given size of polymer stream, the use of the inventive process results in the minimum degree of orientation of the spun fibre as shown by its possessing a relatively low birefringence. Examples relate to the spinning of polyethylene terephthalate and isotactic polypropylene filaments.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB35785/65A GB1088240A (en) | 1965-08-20 | 1965-08-20 | Melt spinning of fibre-forming polymers |
FR73662A FR1495029A (en) | 1965-08-20 | 1966-08-19 | Process for melt-spinning fibrogenic polymers |
NL6611719A NL6611719A (en) | 1965-08-20 | 1966-08-19 | |
US573532A US3492691A (en) | 1965-08-20 | 1966-08-19 | Spinning of fibres |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB35785/65A GB1088240A (en) | 1965-08-20 | 1965-08-20 | Melt spinning of fibre-forming polymers |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1088240A true GB1088240A (en) | 1967-10-25 |
Family
ID=10381530
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB35785/65A Expired GB1088240A (en) | 1965-08-20 | 1965-08-20 | Melt spinning of fibre-forming polymers |
Country Status (3)
Country | Link |
---|---|
US (1) | US3492691A (en) |
GB (1) | GB1088240A (en) |
NL (1) | NL6611719A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4743186A (en) * | 1985-08-31 | 1988-05-10 | Barmag Ag | Melt spinning apparatus |
EP0530652A2 (en) * | 1991-09-06 | 1993-03-10 | Akzo Nobel N.V. | Device for the high-speed spinning of multifilament yarns and its use |
WO1993019229A1 (en) * | 1992-03-18 | 1993-09-30 | Maschinenfabrik Rieter Ag | Process and device for producing continuous synthetic filaments |
EP0580977A1 (en) * | 1992-06-13 | 1994-02-02 | Barmag Ag | Device for spinning synthetic yarns |
US5593705A (en) * | 1993-03-05 | 1997-01-14 | Akzo Nobel Nv | Apparatus for melt spinning multifilament yarns |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3679786A (en) * | 1970-05-21 | 1972-07-25 | Phillips Fibers Corp | Method and apparatus for melt spinning of synthetic filaments |
DE59201340D1 (en) * | 1991-07-23 | 1995-03-16 | Barmag Barmer Maschf | DEVICE FOR PRODUCING A SYNTHETIC THREAD. |
US5688458A (en) * | 1992-03-18 | 1997-11-18 | Maschinenfabrik Rieter Ag | Method and device to manufacture synthetic endless filaments |
DE19535143B4 (en) * | 1994-09-30 | 2006-02-16 | Saurer Gmbh & Co. Kg | Apparatus and method for the thermal treatment of fibers |
CA2411874A1 (en) * | 2000-07-10 | 2002-01-17 | E.I. Du Pont De Nemours And Company | Method of producing polymeric filaments |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3274644A (en) * | 1964-04-27 | 1966-09-27 | Du Pont | Adjustable profile chimney |
NL128276C (en) * | 1964-12-03 | 1970-03-16 | ||
US3313001A (en) * | 1965-09-24 | 1967-04-11 | Midland Ross Corp | Melt spinning apparatus |
-
1965
- 1965-08-20 GB GB35785/65A patent/GB1088240A/en not_active Expired
-
1966
- 1966-08-19 NL NL6611719A patent/NL6611719A/xx unknown
- 1966-08-19 US US573532A patent/US3492691A/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4743186A (en) * | 1985-08-31 | 1988-05-10 | Barmag Ag | Melt spinning apparatus |
EP0530652A2 (en) * | 1991-09-06 | 1993-03-10 | Akzo Nobel N.V. | Device for the high-speed spinning of multifilament yarns and its use |
EP0530652A3 (en) * | 1991-09-06 | 1993-08-11 | Akzo N.V. | Device for the high-speed spinning of multifilament yarns and its use |
US5612063A (en) * | 1991-09-06 | 1997-03-18 | Akzo N.V. | Apparatus for melt spinning multifilament yarns |
WO1993019229A1 (en) * | 1992-03-18 | 1993-09-30 | Maschinenfabrik Rieter Ag | Process and device for producing continuous synthetic filaments |
EP0580977A1 (en) * | 1992-06-13 | 1994-02-02 | Barmag Ag | Device for spinning synthetic yarns |
US5593705A (en) * | 1993-03-05 | 1997-01-14 | Akzo Nobel Nv | Apparatus for melt spinning multifilament yarns |
Also Published As
Publication number | Publication date |
---|---|
US3492691A (en) | 1970-02-03 |
NL6611719A (en) | 1967-02-21 |
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