GB1318024A - Process for obtaining crimped fibres of acrylonitrile copolymers and polymer mixtures - Google Patents
Process for obtaining crimped fibres of acrylonitrile copolymers and polymer mixturesInfo
- Publication number
- GB1318024A GB1318024A GB1142071*[A GB1142071A GB1318024A GB 1318024 A GB1318024 A GB 1318024A GB 1142071 A GB1142071 A GB 1142071A GB 1318024 A GB1318024 A GB 1318024A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fibres
- filaments
- weight
- bath
- acrylonitrile
- 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
- 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
- D01F6/18—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polymers of unsaturated nitriles, e.g. polyacrylonitrile, polyvinylidene cyanide
-
- 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
- D01F6/28—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D01F6/38—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds comprising unsaturated nitriles as the major constituent
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Artificial Filaments (AREA)
Abstract
1318024 Polyacrylonitrile filaments CTACOMPAGNIE INDUSTRIELLE DE TEXTILES ARTIFICIELS ET SYNTHETIQUES 26 April 1971 [24 April 1970] 11420/71 Heading B5B [Also in Division D1] A process for obtaining fibres of acrylonitrile polymers (containing more than 50% by weight of acrylonitrile units) possessing an inherent crimp comprises wet spinning a solution of the acrylonitrile polymer in an organic solvent into a coagulating bath consisting of a mixture of a solvent for the polymer, isopropanol and 0-2% of water; stretching the filaments so formed in a bath consisting of a solvent for the polymer, isopropanol and 0-2% of water and maintained at a temperature 80-95 C.; cutting the filaments to staple length and washing the fibres or the uncut filaments in an untensioned state; giving the fibres a relaxation treatment, without tension; and drying the fibres without tension. The coagulating bath and the stretching bath preferably are of the same composition and comprise 37-49% by weight of solvent, 61- 49% by weight of isopropanol and up to 2% by weight of water. The coagulating bath is maintained at a temperature below 30 C., preferably between 0 and 20 C. In a preferred embodiment, the filaments are given a preliminary stretch in air at ambient temperature prior to the stretching in the bath and at a lower ratio. The filaments are preferably stretched in the bath to a ratio between 5 and 10. The fibres are given a relaxation treatment by immersion in boiling water. The washing step is preferably performed in counter-current. The crimped, dried fibres may be given a heat treatment without tension to prevent or reduce subsequent shrinkage of the fibres. The organic solvents used include dimethylformamide, dimethylacetamide and dimethylsulphoxide. A definition of term 'acrylonitrile polymer' is given in the Specification and comprises copolymers, mixtures of polymers, and graft copolymers containing more than 50% by weight of acrylonitrile units and less than 50% by weight of units of one or more components from a list thereof.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7014955A FR2088772A5 (en) | 1970-04-24 | 1970-04-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1318024A true GB1318024A (en) | 1973-05-23 |
Family
ID=9054520
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1142071*[A Expired GB1318024A (en) | 1970-04-24 | 1971-04-26 | Process for obtaining crimped fibres of acrylonitrile copolymers and polymer mixtures |
Country Status (8)
Country | Link |
---|---|
US (1) | US3737504A (en) |
BE (1) | BE762460A (en) |
BR (1) | BR7102329D0 (en) |
DE (1) | DE2119935A1 (en) |
FR (1) | FR2088772A5 (en) |
GB (1) | GB1318024A (en) |
LU (1) | LU62711A1 (en) |
NL (1) | NL7105471A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4013753A (en) * | 1973-10-09 | 1977-03-22 | Bayer Aktiengesellschaft | Process for the production of spontaneously crimping polyacrylonitrile composite fibres with improved crimp properties |
US4332762A (en) * | 1976-04-29 | 1982-06-01 | E. I. Du Pont De Nemours And Company | Process for preparing a spreadable acrylic fiber tow |
NL177759B (en) * | 1979-06-27 | 1985-06-17 | Stamicarbon | METHOD OF MANUFACTURING A POLYTHYTHREAD, AND POLYTHYTHREAD THEREFORE OBTAINED |
US5902530A (en) * | 1997-12-12 | 1999-05-11 | The Standard Oil Company | Process of making high nitrile composite filaments |
-
1970
- 1970-04-24 FR FR7014955A patent/FR2088772A5/fr not_active Expired
-
1971
- 1971-02-03 BE BE762460A patent/BE762460A/en unknown
- 1971-03-03 LU LU62711D patent/LU62711A1/xx unknown
- 1971-04-20 BR BR2329/71A patent/BR7102329D0/en unknown
- 1971-04-22 NL NL7105471A patent/NL7105471A/xx unknown
- 1971-04-22 US US00136566A patent/US3737504A/en not_active Expired - Lifetime
- 1971-04-23 DE DE19712119935 patent/DE2119935A1/en active Pending
- 1971-04-26 GB GB1142071*[A patent/GB1318024A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
LU62711A1 (en) | 1971-08-20 |
BR7102329D0 (en) | 1973-04-10 |
NL7105471A (en) | 1971-10-26 |
FR2088772A5 (en) | 1972-01-07 |
US3737504A (en) | 1973-06-05 |
DE2119935A1 (en) | 1971-11-04 |
BE762460A (en) | 1971-07-16 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PLNP | Patent lapsed through nonpayment of renewal fees |