GB1148022A - Improvements relating to the production of polyacetal fibres - Google Patents
Improvements relating to the production of polyacetal fibresInfo
- Publication number
- GB1148022A GB1148022A GB5156167A GB5156167A GB1148022A GB 1148022 A GB1148022 A GB 1148022A GB 5156167 A GB5156167 A GB 5156167A GB 5156167 A GB5156167 A GB 5156167A GB 1148022 A GB1148022 A GB 1148022A
- Authority
- GB
- United Kingdom
- Prior art keywords
- polyacetal
- filaments
- temperature
- carried out
- heat treatment
- 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
- D01D10/00—Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
- D01D10/02—Heat treatment
-
- 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
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D01F6/04—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins
- D01F6/06—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins from polypropylene
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Artificial Filaments (AREA)
Abstract
1,148,022. Producing polyacetal fibres. CHEMCELL Ltd. 13 Nov., 1967, No. 51561/67. Addition to 962,231. Heading B5B. Polyacetal fibres having improved elastic recovery are produced by subjecting melt-spun polyacetal filaments which have been drawndown from the spinneret at a ratio of at least 25 but have not been subsequently stretched to a dry heat treatment at a temperature of at least 80‹ C. but below the melting temperature of the polyacetal under such conditions that shrinkage of the filaments occurs. The heat treatment may be carried out at a temperature of 120‹ to 150‹ C. It may be carried out at a temperature about 10‹ C. below the melting temperature of the polyacetal. The filaments may be subjected to the heat treatment while they are free to shrink without restraint. The expression " drawn-down ratio " is defined as the ratio of the cross-sectional area of the filament at the spinning orifice to that of the filament as it is taken up or passes over the first godet or other take-up means. The heat treatment may be carried out on staple fibres produced by cutting the filaments to staple length. When the treatment is carried out on the filaments, they may be held under sufficient tension to limit the shrinkage occurring, e.g. to 5 to 15% of their original length. In an example, polyacetal resin (trioxane/ethylene oxide copolymer containing 2% oxyethylene groups, melt index 2À5) is extruded at 212‹ C. through a spinneret and the extruded filaments cooled with air as they emerge from the spinneret. The loose yarn is then heat treated in an air oven at 150‹ C. for 30 minutes and then allowed to cool to room temperature.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB459661A GB962231A (en) | 1967-11-13 | 1961-02-07 | Process for the production of fibres of improved elastic recovery |
GB5156167A GB1148022A (en) | 1967-11-13 | 1967-11-13 | Improvements relating to the production of polyacetal fibres |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB5156167A GB1148022A (en) | 1967-11-13 | 1967-11-13 | Improvements relating to the production of polyacetal fibres |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1148022A true GB1148022A (en) | 1969-04-10 |
Family
ID=10460494
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB459661A Expired GB962231A (en) | 1961-02-07 | 1961-02-07 | Process for the production of fibres of improved elastic recovery |
GB5156167A Expired GB1148022A (en) | 1967-11-13 | 1967-11-13 | Improvements relating to the production of polyacetal fibres |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB459661A Expired GB962231A (en) | 1961-02-07 | 1961-02-07 | Process for the production of fibres of improved elastic recovery |
Country Status (1)
Country | Link |
---|---|
GB (2) | GB962231A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3330897A (en) * | 1961-02-07 | 1967-07-11 | Chemcell 1963 Ltd | Production of fibers of improved elastic recovery |
US3485906A (en) * | 1967-08-31 | 1969-12-23 | Hercules Inc | Melt spinning elastic polypropylene monofilaments |
-
1961
- 1961-02-07 GB GB459661A patent/GB962231A/en not_active Expired
-
1967
- 1967-11-13 GB GB5156167A patent/GB1148022A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
GB962231A (en) | 1964-07-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2980492A (en) | Process for preparing textile yarns | |
US3137989A (en) | Dyeable bulky yarns based on polypropylene | |
ES488304A1 (en) | Dry-spinning polymer filaments | |
US3408277A (en) | Process and apparatus for producing high-bulk synthetic yarns | |
JPS5584420A (en) | Method of making side by side conjugate fiber with no crimp | |
CA1095675A (en) | Nylon 66 yarn having a soft hand produced by tensioning and heat-treating | |
GB1116823A (en) | Spontaneously crimping composite filaments and yarns | |
GB1175756A (en) | Method of producing Crimped Polypropylene Fibres | |
GB1148022A (en) | Improvements relating to the production of polyacetal fibres | |
US4098776A (en) | Poly(arylene sulfide) fibers | |
US3233023A (en) | Spinning of polypropylene | |
GB1081379A (en) | Process for spinning polyamide filaments | |
GB1293851A (en) | Composite filaments of propylene polymers | |
GB1034401A (en) | Improvements in or relating to the spinning of synthetic fibres | |
US3410940A (en) | Mist spinning process | |
US3560604A (en) | Process for making textured polypropylene filaments | |
GB910864A (en) | Method of producing mixtures of different denier filaments or fibres | |
GB1145818A (en) | Process for producing crimped polypropylene fibres | |
US3382307A (en) | Process for the stretching of polyamidic fibres | |
ATE159770T1 (en) | RAPID SPINNING PROCESS | |
US3443002A (en) | Process for producing crimped filaments | |
US3066008A (en) | Process for producing fibers from copolymers of acrylonitrile and vinylidene chloride | |
GB1174867A (en) | Process for Manufacture of Synthetic Fibers | |
JPS5584416A (en) | Polyester fiber of fine denier and its production | |
US3184821A (en) | Treatment of filamentary material |