GB1006040A - Production of polyacrylonitrile fibres - Google Patents
Production of polyacrylonitrile fibresInfo
- Publication number
- GB1006040A GB1006040A GB22174/64A GB2217464A GB1006040A GB 1006040 A GB1006040 A GB 1006040A GB 22174/64 A GB22174/64 A GB 22174/64A GB 2217464 A GB2217464 A GB 2217464A GB 1006040 A GB1006040 A GB 1006040A
- Authority
- GB
- United Kingdom
- Prior art keywords
- dried
- filaments
- stretched
- sodium thiocyanate
- aqueous sodium
- 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
1,006,040. Polyacrylonitrile filaments. JAPAN EXLAN CO. Ltd. May 28, 1964 [June 5, 1963], No. 22174/64. Heading B5B. In the wet-spinning of polyacrylonitrile filaments, the coagulated polyacrylonitrile filaments containing a proportion by weight of solvent not exceeding 1À5 times the dry weight of polymer are dried until their water content is less than 1À5 times the weight of said solvent, the dried filaments stretched in a medium which will not appreciably extract said solvent, and the stretched filaments washed and dried. Homopolymers of acrylonitrile, copolymers of acrylonitrile with other olefinic monomers, block polymers, graft polymers and mixtures of said polymers may be used. Specified monomers include vinyl acetates vinyl esters of other monocarboxylic acids, acrylic acid, acrylic esters such as methyl acrylate and ethyl acrylate; methacrylic acid, methacrylic esters such as methyl methacrylate; vinyl chloride, vinylidene chloride, styrene, methacrylonitrile, vinylidene cyanide, vinyl pyridine and its substituted derivaties, other vinyl-substituted nitrogen-containing heterocyclic compounds such as vinyl imidazole; aliphatic and aromatic sulphonic acids having an unsaturated bond such as styrene sulphonic acid, allyl sulphonic acid and methallyl sulphonic acid and monoolefinic monomers capable of copolymerizing with acrylonitrile. Pigments, anti-colouring agents, stabilizers, plasticers and other conventional additives may be added to the polymer. The spinning solvent may be an organic solvent having a boiling point higher than that of water, e.g. N,N-dimethyl formamide, N,N,-dimethylacetamide, ethylene carbonate and dimethyl sulphoxide, or a concentrated aqueous solution of an inorganic salt, e.g. sodium thiocyanate, calcium thiocyanate, sodium perchlorate, calcium perchlorate, zinc chloride or lithium chloride. Coagulating baths specified include dilute aqueous solutions of the spinning solvent or non-solvents for the polymer and coagulation may be effected at room temperature. Stretching is preferably effected in hot air and washing in water. Crimping, application of finishing agents and cutting are then carried out, and the fibres dried. In Examples: (1) an acrylonitrile/ methyl acrylate/methacryl sulphonic acid copolymer is dissolved in 46% aqueous sodium thiocyanate and spun into 12% aqueous sodium thiocyanate at 20 C. The coagulated filaments are immersed in 4% aqueous sodium thiocyanate, removed, dried in air at 50 C., stretched in hot air, washed in cold water and dried at 150 C. (2) Coagulated gel filaments made as in (1) are immersed in 5% aqueous sodium thiocyanate, removed, dried, stretched in hot water, washed in hot water and dried at 105 C. (3) An acrylonitrile/methyl acrylate copolymer is dissolved in 50% aqueous sodium thiocyanate and spun into 75% aqueous sodium thiocyanate at 15 C. The coagulated filaments are dried at 50 C., stretched in hot air at 105 C., washed in cold water and dried at 105 C. (4) Dried gel filaments made as in (2) but before being subjected to stretching are stretched while being heated between infra-red lamps, washed with water and dried at 105 C. In general, stretch ratios of 5À3-9À9 and stretching temperatures of 60-200 C. are used. Filaments so made are dense, have a smooth surface, circular cross-section and a silk-like touch and lustre.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2944563 | 1963-06-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1006040A true GB1006040A (en) | 1965-09-29 |
Family
ID=12276305
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB22174/64A Expired GB1006040A (en) | 1963-06-05 | 1964-05-28 | Production of polyacrylonitrile fibres |
Country Status (7)
Country | Link |
---|---|
US (1) | US3399260A (en) |
BE (1) | BE646691A (en) |
DE (1) | DE1494623A1 (en) |
FR (1) | FR1397075A (en) |
GB (1) | GB1006040A (en) |
LU (1) | LU46167A1 (en) |
NL (1) | NL6405582A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113758887A (en) * | 2021-08-20 | 2021-12-07 | 北京化工大学 | Method for screening extractants and testing residual solvent dimethyl sulfoxide in polyacrylonitrile precursors |
CN116024674A (en) * | 2021-10-26 | 2023-04-28 | 中国石油化工股份有限公司 | Method for preparing polyacrylonitrile nascent fiber by gel spinning and nascent fiber thereof |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3485913A (en) * | 1965-10-20 | 1969-12-23 | Toho Beslon Co | New method of manufacturing acrylic fibers and the related products |
JPS52870A (en) * | 1975-06-24 | 1977-01-06 | Kureha Chemical Ind Co Ltd | Method of prevention or recovery of whitening of formed product of acrylonitrile polymer due to absorption of water |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2697023A (en) * | 1950-04-29 | 1954-12-14 | Eastman Kodak Co | Spinning acrylonitrile |
US2948581A (en) * | 1955-12-20 | 1960-08-09 | American Cyanamid Co | Method of producing a synthetic fiber |
US2984912A (en) * | 1958-08-14 | 1961-05-23 | American Cyanamid Co | Art of producing filamentary polyacrylonitrile |
NL245712A (en) * | 1958-11-24 | 1900-01-01 | ||
US3052512A (en) * | 1960-06-14 | 1962-09-04 | American Cyanamid Co | Art of producing polyacrylonitrile filamentary materials |
US3101245A (en) * | 1960-08-18 | 1963-08-20 | American Cyanamid Co | Production of polyacrylonitrile fibers |
BE629770A (en) * | 1962-03-19 |
-
1964
- 1964-04-17 BE BE646691D patent/BE646691A/xx unknown
- 1964-05-20 NL NL6405582A patent/NL6405582A/xx unknown
- 1964-05-27 US US370722A patent/US3399260A/en not_active Expired - Lifetime
- 1964-05-27 LU LU46167D patent/LU46167A1/xx unknown
- 1964-05-28 GB GB22174/64A patent/GB1006040A/en not_active Expired
- 1964-06-03 FR FR976953A patent/FR1397075A/en not_active Expired
- 1964-06-04 DE DE19641494623 patent/DE1494623A1/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113758887A (en) * | 2021-08-20 | 2021-12-07 | 北京化工大学 | Method for screening extractants and testing residual solvent dimethyl sulfoxide in polyacrylonitrile precursors |
CN113758887B (en) * | 2021-08-20 | 2022-11-29 | 北京化工大学 | Method for screening extracting agent and testing residual solvent dimethyl sulfoxide in polyacrylonitrile protofilament |
CN116024674A (en) * | 2021-10-26 | 2023-04-28 | 中国石油化工股份有限公司 | Method for preparing polyacrylonitrile nascent fiber by gel spinning and nascent fiber thereof |
Also Published As
Publication number | Publication date |
---|---|
FR1397075A (en) | 1965-04-23 |
US3399260A (en) | 1968-08-27 |
BE646691A (en) | 1964-10-19 |
DE1494623A1 (en) | 1969-07-03 |
LU46167A1 (en) | 1972-01-01 |
NL6405582A (en) | 1964-12-07 |
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