US2970884A - Modified acrylonitrile polymer fibers with increased shrinkability and dyeability - Google Patents

Modified acrylonitrile polymer fibers with increased shrinkability and dyeability Download PDF

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US2970884A
US2970884A US733623A US73362358A US2970884A US 2970884 A US2970884 A US 2970884A US 733623 A US733623 A US 733623A US 73362358 A US73362358 A US 73362358A US 2970884 A US2970884 A US 2970884A
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fiber
aquagel
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acrylonitrile
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George W Stanton
Armen Ardy
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Dow Chemical Co
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/02Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/18Monocomponent 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
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F11/00Chemical after-treatment of artificial filaments or the like during manufacture
    • D01F11/04Chemical after-treatment of artificial filaments or the like during manufacture of synthetic polymers
    • D01F11/06Chemical after-treatment of artificial filaments or the like during manufacture of synthetic polymers of macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/28Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/38Monocomponent 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

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  • This invention is germane to the general field of organic chemistry and contributes especially to the polymer art. More specifically, the present invention has reference to shaped articles, particularly fibers and related filamentous structures, which are comprised of essentially linear acrylonitrile polymer compositions which have been modified while they are in an already-fabricated form in order to improve or increase their shrinkability and dyeability, which polymers contain in their molecule recurring alkyl acrylamide units.
  • Polyacrylonitrile and many of the fiber-forming copolymers of acrylonitrile may advantageously be fabricated into synthetic textile fibers by a wet spinning process of a known variety wherein the fiber-forming polymer composition is salt spun using polyacrylonitrile-dissolving aqueous saline solvents, particularly Zinc chloride and its saline equivalents, for preparation of the spinning solution or other composition and non-polymer-dissolving coagulating spin bath solutions of the same salt or salts during the wet spinning operation.
  • Acrylonitrile polymers, particularly polyacrylonitrile, that are wet spun in such manner are generally formed as aquagel intermediates.
  • Suchintermediates have a water-swollen or hydrated structure prior to their being finally irreversibly dried to the desired, characteristically hydrophobic, textile fiber product.
  • These aquagels. generally contain an amount of water that is at least gravimetrically equal to the hydrated polymer that is contained therein. It may oftentimes be preferable for the Water-to-polymer weight ratio in the aquagel to be in the neighborhood of from about 1.5 :l to 2.021, respectively. Aquagel structures in which the water-to-polymer ratio prior to irreversible drying and during their manufacturing process is as high as 4.5 or :1 may frequently be satisfactorily employed.
  • aquagel structures of polyacrylonitrile and other fiber-forming acrylonitrile polymers may be derived by the extrusion into and coagulation in an aqueous coagulating spin bath of a solution of the acrylonitrile polymer that is dissolved in an aqueous zinc chloride saline solvent therefor.
  • zinc chloride it is usually desirable for zinc chloride to be at least the principal (if not the entire) saline solute in the aqueous saline solvent solution. If preferred, however, various of the saline equivalents for zinc chloride may also be employed in the aqueous saline solvent medium for the spinning solution and the coagulating bath utilized.
  • Synthetic acrylonitrile polymer fibers derived from aquagels in salt spinning processes generally have a normal shrinkage of between about 12 and 14 percent. For most purposes the indicated order of shrinkage is quite satisfactory. It may'frequently be deemed ad vantageous and desirable, however, for synthetic fibers to be available having greater shrinkability. Thus, in the preparation of high-bulk yarns, it is beneficial to combine fibers of high shrinkability with others of relatively low shrinkabiltyi When the mixed fibers in the yarn butyl alcohol of the. structure:
  • each R independently has from 1 to about 4 construction (or in cloth or fabric manufactured from such yarn) are shrunk together, the variation of shrinkage properties produce partial bending and loop formation in the longer fibers. This results in a yarn of high bulk and softness. Textile goods of such characteristics are frequently of great desirability for the manufacture of such articles as sweaters, comforters, scarfs, etc.
  • the chief aim and concern of the present invention is to provide synthetic acrylonitrile polymer textile fibers prepared by the indicated salt-spinning process which have generally greater shrinkability than the conventional acrylonitrile polymer fibers that are derive-d from aquagel intermediates in Wet spinning operations.
  • Another design and object of the present invention is to provide synthetic acrylonitrile polymer fibers having enhanced receptivity to many of a wide variety of dyestuffs.
  • dye-receptive, high-shrinkable synthetic acrylonitrile polymer textile fibers derived from aquagels that have been salt spun in the indicated manner may be obtained b a method in accordance with the present invention which, surprisingly and simply enough, comprises impregnating (or subjecting to intimate physical contact) an already formed, and at least partially oriented by stretching, acrylonitrile polymer fiber in aquagel form to solutions or dispersions of certain alcohols (or their mixtures) in a polar, preferably aqueous, medium in the simultaneous or subsequent presence of strong aqueous acid solutions; then washing the treated aquagel free from the treating reagents; and subsequently irreversibly drying the treated aquagel to the desired characteristically hydrophobic, synthetic textile fiber product having increased shrinkability and enhanced dye-receptivity.
  • the fibers treated in accordance with the present invention have a shrinkability (as when subjected to steam or boiling water after their irreversible drying) of between about 16 and 18 percent.
  • the finally obtained fibers can be shrunk by steam or in boiling water by as much as 16-18 percent of the original length in which they were obtained after their final irreversible drying from the aquagel condition.
  • Such fibers one of which is schematically portrayed in the sole figure of the accompanying drawing, can advantageously be interblended with normally manufactured acrylonitrile polymer or other varieties of synthetic textile fibers having less inherent shrinkability in order to advantageously prepare high-bulk yarn constructions.
  • the treated-fibers are also rendered more dyeable with many diverse types of dyestuffs including vat dyes, sulfur dyes, direct dyes, acid dyes, basic dyes, premetalized dyestuffs and the like that frequently are not particularly effective on acrylonitrile polymer fibers, especially fibers consisting entirely of polyacrylonitrile.
  • dyestuffs including vat dyes, sulfur dyes, direct dyes, acid dyes, basic dyes, premetalized dyestuffs and the like that frequently are not particularly effective on acrylonitrile polymer fibers, especially fibers consisting entirely of polyacrylonitrile.
  • the alcohols that may be utilized in the practice of the present invention include tertiary alcohols of the generic structure:
  • R3COH (I) carbon atoms with the limitation that the total number of carbon atoms in all three R substituents is from 3 to 7 and benzyl alcohols of the general structure:
  • each X is independently selected from the group consisting of hydrogen, chlorine, bromine or an alkyl radical containing from 1 to about 4 carbon atornsand n has a whole numbervalue from 0 to 5.
  • tertlar amyl alcohol of the structure C H (CH C0H; tertiary- (CH COH; fi-methyl-i Patented Feb.
  • tertiary-amyl alcohol tertiary-butyl alcohol, or benzyl alcohol are employed.
  • the alcohols can be employed in either solution or dispersion in order to impregnate the aquagel structure therewith for accomplishment of the desired modification.
  • sulfuric acid in aqueous solutions having a concentration of from 40 to 95 percent, advantageously from 60 to 90 percent, and more advantageously aoout 70 percent by weight of H SO4.
  • other strongly dissociated inorganic acids of equivalent strength in aqueous solution to the mentioned sulfuric acid may also be utilized, particularly such acids as hydrochloric acid.
  • the treatment may be accomplished by impregnating the Washed and oriented aquagel fiber in an aqueous or undiluted bath of the alcohol followed by acid treatment.
  • the aquagel fiber can be treated in a single bath containing a mixture of the alcohol and acid.
  • the aquagel fiber is impregnated during the treatment with a sufficient quantity of the alcohol to convert between about 5 and 25 mole percent, preferably between about 8 and mole percent, of the substituent nitrile groups in the acrylonitrile polymer structure to alkyl amide groups so as, in effect, to obtain a copolymer containing between about 75 and 95 mole percent of recurring units derived from acrylonitrile of the structure:
  • the precise quantity of alcohol impregnated in the aquagel depends upon the amount of water permitted to remain in the aquagel structure before the impregnation step as well as the particular alcohol being utilized for the modifying operationin many cases, however, an amount of alcohol between about 5 and 50 percent by weight, based on'theweight of an aquagel containing about 2 parts of water to each part of dry polymer therein, will provide satisfactory and beneficial results inthe practice of the invention.
  • the conversion may be eilected at any temperature between about (F15 and, 110 0., although it is generally most convenient and quite'satisfactory to accomplish the modification at about room temperature or in the range between about 20 and C.
  • the necessary time for accomplishing the rnodification depends upon the temperature employed and the quantity of alcohol inthe aquagel fiber. Generally,:the treatment can be accomplished within 24-48 hours and,
  • reaction-favpring conditions under'optimum reaction-favpring conditions, is usually performable in. as little as 5-l minutes.
  • the treated fiber is irreversibly dried to produce the desired high-shrink and dyeable, characteristically hydrophobic, synthetic textile fiber product.
  • acrylonitrile polymer aquagels may be irreversibly dried most satisfactorily at temperatures between about 100 and 150 C. for periods of time between about 30 and 5 minutes.
  • the dyeable, high-shrink fiber product of the present invention may advantageously be incorporated in blends with low shrinking fibers of the same or other general varieties in order to produce high bulk yarn constructions.
  • the fiber product of the present invention may be blended with lower shrinking fibers of polyacrylonitrile or other fiber-forming acrylonitrile polymers or with lower shrinking fibers of other materials, including fibers of nylon, polyesters (Dacron) etc.
  • the quantity of high shrink fiber that is incorporated in the blend for such yarn constructions depends upon the bulking eifect desired in the final product. Greater relative proportions of the high shrink product ordinarily cause relatively less bulking in the blended yarn. Generally, an amount of between about 30 and weight percent of the high shrink fiber blended with the conventional low shrinking fiber provides satisfactory results.
  • polyacrylonitrile aquagels it is ordinarily most desirable to employ and modify polyacrylonitrile aquagels in the practice of the present invention. If desired, however, certain of the fiber-forming copolymers and graft copolymers of acrylonitrile and graft copolymers on polyacrylonitrile can be utilized in place of polyacrylonitrile including those which form fibers having the same tendency for shrinkage as homopolymeric acrylonitrile.
  • the acrylonitrile polymers that are modified by practice of the present invention can be high polymers having'a molecular weight in the range (say, roughly from 25 to 60 thousand or so) that is generally contemplated by those skilled in the art as being most desirable for fiber-forming acrylonitrile polymers;
  • the aquagel structures that are modified by the present practice can also be utilized when they contain interblended therewith up to about 20 weight percent of various dye-assisting polymeric adjuvants, including poly- N-vinyl-pyrrolidone and the like or equivalent dyereceptors, that have been blended in the aquagel structure by extrusion of a fiber-forming polymer blend or by impregnation of the dye-assisting adjuvant after initial fabrication of the aquagel.
  • modified aquagels may also, if desired, be further impregnated prior to their final irreversible drying with polymeric dye-assisting adjuvants or other beneficial treating agents for the fibrous product.
  • a spinning solution comprised of about 10 parts of polyacrylonitrile dissolved in about parts of a 60 percent aqueous solution of zinc chloride was salt-spun by being extruded through a spinnerette having 750 individual orifices, each of which had a diameter of about 6 mils,- into an aqueous coagulating bath that contained about 7 42 weight percent of zinc chloride dissolved therein to be spun into a multiple filament aquagel tow.
  • agulated tow was washed substantially free from salt after being withdrawn from the coagulating bath and oriented by being stretched to a length of about 12 times its original extruded length prior to being collected or dried. There was thereby obtained an aquagel fiber containing about 2 parts of water for each part of polymer therein.
  • Several samples of the polyacrylonitrile aquageL each containing about 10 grams on a dry weight basis of the polymer, were then individually wound'on separate, perforated stainless steel cylinders. Each of the samplesl'excepting for two control samples.) were then immersed in individual 500 ml. baths of various. alcohols for about. one hour at room temperature. After this, the samples were removed and permitted todrain before subsequently being immersed in 500 ml.
  • each of the modified aquagel fiber samples were washed several times with distilled water until no trace of residual acidcould be noted. They were then irreversibly dried for 5 minutes at 140 C. and tested for shrinkability.
  • samples 1 and 7 are blanks which received no treatment and samples 2 and 8 were treated merely by immersion in the acid without prior alcohol impregnation.
  • Samples 6 and 12 employed an alcohol not in accordance with the present invention for purposes of additional comparison.
  • the shrinkability of the fiber samples was determined according to the following tests:
  • polymers prepared by other methods adapted to provide about the same chemical composition in the resulting fiber did not produce fibers that evidenced any noticeable increase in shrinkability.
  • the resulting textile fiber products had about the same order of shrinkability as the untreated fiber samples illustrated in samples 1 and 7.
  • the spinning solution was prepared to pH 3 (measured at 10:1 dilution in distilled water) with HCl before solution polymerization of the monomer to pro vide the fiber-forming polymer composition.
  • two fiber-forming acrylonitrile copolyrners were prepared, each containing about 91 weight percent of acrylonitrile copolymerized in the polymer molecule.
  • One of the comonomers utilized was N-t-butylacrylamide.
  • the other was N-t-octylacrylamide.
  • Method of preparing a dye-receptive and highly shrinkable synthetic acrylonitrile polymer textile fiber which method comprises salt spinning a fiber-forming acrylonitrile polymer that is adapted to provide fibers which do not shrink more than 14 percent after exposure to water at about C., which polymer contains in the polymer molecule at least about 80 weight percent of acrylonitrile, any balance being another monoethylenioally unsaturated monomeric material that is copolymerizable with acrylonitrile, into an aquagel filamentary structure that contains between about 1 and 5 parts by Weight of water to each part by weight of dry polymer therein; washing said aquagel substantially free from residual salt and physically elongating said fiber by stretching it to an at least partially oriented condition; subjecting said aquagel fiber to intimate contact with (a) at least one alcohol selected from the group consisting of tertiary alcohols and benzyl alcohols having the respective formulae:
  • each R in said tertiary alcohol is an independently selected alkyl radical that contains from 1 to about 4 7 carbon atoms with the limitation that the total number of carbon atoms in all three substituents is from 3 to 7; and wherein each X in said benzyl alcohol is selected from the group consisting of hydrogen, chlorine, bromine and al'kyl radicals containing from 1 to about 4 carbons and n has a whole number value from to 5, said alcohol being employed in sufiicient quantity to convert between about 5 and 25 mole percent of the nitrile groups in said acrylonitrile polymer to acrylamide substituents; and (b) an aqueous solution of a strong dissociated inorganic acid containing about 40 to 95 percent by weight of the acid and selected from the group consisting of sulfuric acid, hydrochloric acid, and their mixtures; maintaining said aquagel in contact with said acid solution at a temperature between about 0 and 110 C.

Description

United States Patent MODIFIED ACRYLONITRILE POLYMER FIBERS WITH INCREASED *SHRINKABILITY AND DYE- ABILITY George W. Stanton, Walnut Creek, and Ardy Armen,
Concord, Calif., assignors to The Dow Chemical Company, Midland, Mich., a corporation of Delaware Filed May 7, 1958, Ser. No. 733,623 9 Claims. (Cl. 18-54) This invention is germane to the general field of organic chemistry and contributes especially to the polymer art. More specifically, the present invention has reference to shaped articles, particularly fibers and related filamentous structures, which are comprised of essentially linear acrylonitrile polymer compositions which have been modified while they are in an already-fabricated form in order to improve or increase their shrinkability and dyeability, which polymers contain in their molecule recurring alkyl acrylamide units.
Polyacrylonitrile and many of the fiber-forming copolymers of acrylonitrile may advantageously be fabricated into synthetic textile fibers by a wet spinning process of a known variety wherein the fiber-forming polymer composition is salt spun using polyacrylonitrile-dissolving aqueous saline solvents, particularly Zinc chloride and its saline equivalents, for preparation of the spinning solution or other composition and non-polymer-dissolving coagulating spin bath solutions of the same salt or salts during the wet spinning operation. Acrylonitrile polymers, particularly polyacrylonitrile, that are wet spun in such manner are generally formed as aquagel intermediates. Suchintermediates have a water-swollen or hydrated structure prior to their being finally irreversibly dried to the desired, characteristically hydrophobic, textile fiber product. These aquagels. generally contain an amount of water that is at least gravimetrically equal to the hydrated polymer that is contained therein. It may oftentimes be preferable for the Water-to-polymer weight ratio in the aquagel to be in the neighborhood of from about 1.5 :l to 2.021, respectively. Aquagel structures in which the water-to-polymer ratio prior to irreversible drying and during their manufacturing process is as high as 4.5 or :1 may frequently be satisfactorily employed. Advantageously, aquagel structures of polyacrylonitrile and other fiber-forming acrylonitrile polymers may be derived by the extrusion into and coagulation in an aqueous coagulating spin bath of a solution of the acrylonitrile polymer that is dissolved in an aqueous zinc chloride saline solvent therefor. It is usually desirable for zinc chloride to be at least the principal (if not the entire) saline solute in the aqueous saline solvent solution. If preferred, however, various of the saline equivalents for zinc chloride may also be employed in the aqueous saline solvent medium for the spinning solution and the coagulating bath utilized. These, as is' well known, include various of the thiocyanates (such as calcium thiocyanate), lithium bromide and the salt mixtures that are members of the so-called lyotropic series. Such aqueous saline solvents for polyacrylonitrile have been disclosed, among other places, in United States Letters Patents Nos. 2,140,921; 2,425,192; 2,648,592; 2,648,593; 2,648,646; 2,648,648gand 2,648,649. r i
Synthetic acrylonitrile polymer fibers derived from aquagels in salt spinning processes generally have a normal shrinkage of between about 12 and 14 percent. For most purposes the indicated order of shrinkage is quite satisfactory. It may'frequently be deemed ad vantageous and desirable, however, for synthetic fibers to be available having greater shrinkability. Thus, in the preparation of high-bulk yarns, it is beneficial to combine fibers of high shrinkability with others of relatively low shrinkabiltyi When the mixed fibers in the yarn butyl alcohol of the. structure:
wherein each R independently has from 1 to about 4 construction (or in cloth or fabric manufactured from such yarn) are shrunk together, the variation of shrinkage properties produce partial bending and loop formation in the longer fibers. This results in a yarn of high bulk and softness. Textile goods of such characteristics are frequently of great desirability for the manufacture of such articles as sweaters, comforters, scarfs, etc.
The chief aim and concern of the present invention is to provide synthetic acrylonitrile polymer textile fibers prepared by the indicated salt-spinning process which have generally greater shrinkability than the conventional acrylonitrile polymer fibers that are derive-d from aquagel intermediates in Wet spinning operations. Another design and object of the present invention is to provide synthetic acrylonitrile polymer fibers having enhanced receptivity to many of a wide variety of dyestuffs.
To the attainment of the indicated and corollary ends, dye-receptive, high-shrinkable synthetic acrylonitrile polymer textile fibers derived from aquagels that have been salt spun in the indicated manner may be obtained b a method in accordance with the present invention which, surprisingly and simply enough, comprises impregnating (or subjecting to intimate physical contact) an already formed, and at least partially oriented by stretching, acrylonitrile polymer fiber in aquagel form to solutions or dispersions of certain alcohols (or their mixtures) in a polar, preferably aqueous, medium in the simultaneous or subsequent presence of strong aqueous acid solutions; then washing the treated aquagel free from the treating reagents; and subsequently irreversibly drying the treated aquagel to the desired characteristically hydrophobic, synthetic textile fiber product having increased shrinkability and enhanced dye-receptivity. Generally, the fibers treated in accordance with the present invention have a shrinkability (as when subjected to steam or boiling water after their irreversible drying) of between about 16 and 18 percent. Thus, the finally obtained fibers can be shrunk by steam or in boiling water by as much as 16-18 percent of the original length in which they were obtained after their final irreversible drying from the aquagel condition. Such fibers, one of which is schematically portrayed in the sole figure of the accompanying drawing, can advantageously be interblended with normally manufactured acrylonitrile polymer or other varieties of synthetic textile fibers having less inherent shrinkability in order to advantageously prepare high-bulk yarn constructions. The treated-fibers are also rendered more dyeable with many diverse types of dyestuffs including vat dyes, sulfur dyes, direct dyes, acid dyes, basic dyes, premetalized dyestuffs and the like that frequently are not particularly effective on acrylonitrile polymer fibers, especially fibers consisting entirely of polyacrylonitrile.
The alcohols that may be utilized in the practice of the present invention include tertiary alcohols of the generic structure:
R3COH (I) carbon atoms with the limitation that the total number of carbon atoms in all three R substituents is from 3 to 7 and benzyl alcohols of the general structure:
@otnon wherein each X is independently selected from the group consisting of hydrogen, chlorine, bromine or an alkyl radical containing from 1 to about 4 carbon atornsand n has a whole numbervalue from 0 to 5. Thus, amongst-- the various alcohols which may be employed are tertlar amyl alcohol of the structure: C H (CH C0H; tertiary- (CH COH; fi-methyl-i Patented Feb. 7, 1961 V pentane-3-ol of the structure: (C H CH COH; 2- rnethyl-pentane-2-ol of the structure: C H (CH COH; 3-ethyl-pentane-3-ol of the structure: (C H COH; 3- methyl-heXane-3-ol of the structure: C H C H CI-I COH; Z-methyl-hexaneQ-ol of the structure: C H (CH COH; p-chloro-benzyl alcohol; 2,4-dibromo-benzyl alcohol; 2- chlo'robmethyl-benzyl alcohol; and the like. Advantageously, tertiary-amyl alcohol, tertiary-butyl alcohol, or benzyl alcohol are employed. As indicated, the alcohols can be employed in either solution or dispersion in order to impregnate the aquagel structure therewith for accomplishment of the desired modification.
Among the acids that. may be utilized with utmost benefit is sulfuric acid in aqueous solutions having a concentration of from 40 to 95 percent, advantageously from 60 to 90 percent, and more advantageously aoout 70 percent by weight of H SO4. if desired, other strongly dissociated inorganic acids of equivalent strength in aqueous solution to the mentioned sulfuric acid may also be utilized, particularly such acids as hydrochloric acid.
The treatment may be accomplished by impregnating the Washed and oriented aquagel fiber in an aqueous or undiluted bath of the alcohol followed by acid treatment. Alternatively, and with equal advantage, the aquagel fiber can be treated in a single bath containing a mixture of the alcohol and acid. Beneficially, the aquagel fiber is impregnated during the treatment with a sufficient quantity of the alcohol to convert between about 5 and 25 mole percent, preferably between about 8 and mole percent, of the substituent nitrile groups in the acrylonitrile polymer structure to alkyl amide groups so as, in effect, to obtain a copolymer containing between about 75 and 95 mole percent of recurring units derived from acrylonitrile of the structure:
l H 'H. \C r-C and from about 5 to mole percent of'recurring alkyl acrylamide units of the structure:
(llOfifl'Z OH H- C 1, wherein Z, as is apparent, is a substituent whose precise characteristics depend upon the particular alcohol used for modification of the acrylonitrile polymer. Thus, when alcohols of Formula I are involved Z is CR with benzyl alcohols it is:
II As will be evident to those who are skilled in the art, the precise quantity of alcohol impregnated in the aquagel depends upon the amount of water permitted to remain in the aquagel structure before the impregnation step as well as the particular alcohol being utilized for the modifying operationin many cases, however, an amount of alcohol between about 5 and 50 percent by weight, based on'theweight of an aquagel containing about 2 parts of water to each part of dry polymer therein, will provide satisfactory and beneficial results inthe practice of the invention. The conversion may be eilected at any temperature between about (F15 and, 110 0., although it is generally most convenient and quite'satisfactory to accomplish the modification at about room temperature or in the range between about 20 and C. The necessary time for accomplishing the rnodification depends upon the temperature employed and the quantity of alcohol inthe aquagel fiber. Generally,:the treatment can be accomplished within 24-48 hours and,
,under'optimum reaction-favpring conditions, is usually performable in. as little as 5-l minutes.
After the treatment, the modified acrylonitrile poly.
melz aqua'gel fiben Washed thoroughly with water-{to remove all or substantially all of the treating reagents, taking particular care to rid the aquagel of any residual acid. Following the washing, the treated fiber is irreversibly dried to produce the desired high-shrink and dyeable, characteristically hydrophobic, synthetic textile fiber product. Ordinarily, acrylonitrile polymer aquagels may be irreversibly dried most satisfactorily at temperatures between about 100 and 150 C. for periods of time between about 30 and 5 minutes.
After drying, the dyeable, high-shrink fiber product of the present invention may advantageously be incorporated in blends with low shrinking fibers of the same or other general varieties in order to produce high bulk yarn constructions. Thus, the fiber product of the present invention may be blended with lower shrinking fibers of polyacrylonitrile or other fiber-forming acrylonitrile polymers or with lower shrinking fibers of other materials, including fibers of nylon, polyesters (Dacron) etc. The quantity of high shrink fiber that is incorporated in the blend for such yarn constructions depends upon the bulking eifect desired in the final product. Greater relative proportions of the high shrink product ordinarily cause relatively less bulking in the blended yarn. Generally, an amount of between about 30 and weight percent of the high shrink fiber blended with the conventional low shrinking fiber provides satisfactory results.
it is ordinarily most desirable to employ and modify polyacrylonitrile aquagels in the practice of the present invention. If desired, however, certain of the fiber-forming copolymers and graft copolymers of acrylonitrile and graft copolymers on polyacrylonitrile can be utilized in place of polyacrylonitrile including those which form fibers having the same tendency for shrinkage as homopolymeric acrylonitrile. In this connection, it is advantageous for the acrylonitrile polymers that are modified by practice of the present invention to be high polymers having'a molecular weight in the range (say, roughly from 25 to 60 thousand or so) that is generally contemplated by those skilled in the art as being most desirable for fiber-forming acrylonitrile polymers; In addition, the aquagel structures that are modified by the present practice can also be utilized when they contain interblended therewith up to about 20 weight percent of various dye-assisting polymeric adjuvants, including poly- N-vinyl-pyrrolidone and the like or equivalent dyereceptors, that have been blended in the aquagel structure by extrusion of a fiber-forming polymer blend or by impregnation of the dye-assisting adjuvant after initial fabrication of the aquagel.
Likewise, the modified aquagels may also, if desired, be further impregnated prior to their final irreversible drying with polymeric dye-assisting adjuvants or other beneficial treating agents for the fibrous product.
In order to further illustrate the invention, a spinning solution comprised of about 10 parts of polyacrylonitrile dissolved in about parts of a 60 percent aqueous solution of zinc chloride was salt-spun by being extruded through a spinnerette having 750 individual orifices, each of which had a diameter of about 6 mils,- into an aqueous coagulating bath that contained about 7 42 weight percent of zinc chloride dissolved therein to be spun into a multiple filament aquagel tow. The co-,
agulated tow was washed substantially free from salt after being withdrawn from the coagulating bath and oriented by being stretched to a length of about 12 times its original extruded length prior to being collected or dried. There was thereby obtained an aquagel fiber containing about 2 parts of water for each part of polymer therein. Several samples of the polyacrylonitrile aquageL each containing about 10 grams on a dry weight basis of the polymer, were then individually wound'on separate, perforated stainless steel cylinders. Each of the samplesl'excepting for two control samples.) were then immersed in individual 500 ml. baths of various. alcohols for about. one hour at room temperature. After this, the samples were removed and permitted todrain before subsequently being immersed in 500 ml. baths of 70 percent aqueous sulfuric acid for 30 minutes at about24 C. During the acid immersion, the temperature of each of the acid solutions was noted to rise about half a centigrade degree. After the acid treatments, each of the modified aquagel fiber samples were washed several times with distilled water until no trace of residual acidcould be noted. They were then irreversibly dried for 5 minutes at 140 C. and tested for shrinkability.
Several additional samples of aquagel fiber were similarly prepared and treated excepting that each of the samples contained about percent by weight, based on the dry weight of the polymer therein, of K-54 poly-N- vinyl-2-pyrrolidone (PVP) which was incorporated therein by impregnation from an aqueous bath in order to improve the dye-receptivity of the finally obtained fiber structure.
The results are set forth in the following tabulation, wherein samples 1 and 7 are blanks which received no treatment and samples 2 and 8 were treated merely by immersion in the acid without prior alcohol impregnation. Samples 6 and 12 employed an alcohol not in accordance with the present invention for purposes of additional comparison.
The shrinkability of the fiber samples was determined according to the following tests:
Determination of shrinkage of treated fibers-The dried fiberjn tow form was stretched to 1.25 times its original length by passing it between two electrically heated aluminum plates 6 inches long. The plates were set about 7 inch apart and were heated to 175 C. The linear speed of the tow entering the stretching zone was 30.5 feet per minute. The fibers stretched under these conditions were shrunk in a steam chamber by the following steaming cycle:
(a) One minute purge at atmospheric pressure (b) One minute to raise pressure to 10 p.s.i.g.
(c) Two minutes to hold at 10 p.s.i.g.
(d) Fifteen seconds to release to atmospheric pressure The steam shrunk fibers were dried at 40 C. The initial length of the fiber tow to be shrunk was 90 cm. The distance was marked on the tow sample by tying two pieces of string about the tow, 90 cm. apart, while the tow was under a tension of about 0.1 gm. per denier. After shrinking, the tow was again put under a tension of 0.1 gram per denier and the distance between the markers measured. The shrinkage was then calculated by the following formula:
Original length-final length Original length X100 Percent; shrink:
The percent shrink values were usually reproducible to 20.2 percent.
TABLE I Shrinkage properties of polyacrylonitrile wet-stretched gel treated with various alcohols and sulfuric acid 1 Impregnated with PVP before treatment.
Similar results are obtained when the foregoing is re peated excepting to use mixed acid-alcohol baths for the modifying treatment or to utilize other of thealcohols and acids indicated to be within the scope of the invention, as well as when aquagels spun from other salt systems (including any of those mentioned in the fore going) are treated.
In contrast with the foregoing, polymers prepared by other methods adapted to provide about the same chemical composition in the resulting fiber did not produce fibers that evidenced any noticeable increase in shrinkability. Thus, when polyacrylonitrile was reacted with tertiary butyl alcohol while the polymer was dissolved in the aqueous 60 percent zinc chloride spinning solution containing about 10 percent by weight of the fiber-forming polymer, the resulting textile fiber products had about the same order of shrinkability as the untreated fiber samples illustrated in samples 1 and 7. In these experiments, the spinning solution was prepared to pH 3 (measured at 10:1 dilution in distilled water) with HCl before solution polymerization of the monomer to pro vide the fiber-forming polymer composition. Ten percent by weight of tertiary butyl alcohol was added to several samples of the polymer solution, based on the Weight of the polyacrylonitrile dissolved therein. The alcohol was added as an equal weight solution with 60 percent aqueous zinc chloride to prevent coagulation of the polymer solution. The reaction of the alcohol with the polyacrylonitrile was accomplished at temperatures between 60 and C. None of the filamentary or film materials produced by salt-spinning of such' modified fiber-forming compositions prepared finally manufactured products that showed more than about 12-14 percent shrinkability.
In another series of experiments, two fiber-forming acrylonitrile copolyrners were prepared, each containing about 91 weight percent of acrylonitrile copolymerized in the polymer molecule. One of the comonomers utilized was N-t-butylacrylamide. The other was N-t-octylacrylamide. When fibers were prepared from each of the copolymers in accordance with the above described salt spinning process, the resulting products exhibited shrinkage properties 110 different from untreated polyacrylonitrile fibers.
The scope and purview of the present invention is to be gauged in the light of the hereto appended claims rather than from the foregoing didactic description and specification.
What is claimed is:
1. Method of preparing a dye-receptive and highly shrinkable synthetic acrylonitrile polymer textile fiber which method comprises salt spinning a fiber-forming acrylonitrile polymer that is adapted to provide fibers which do not shrink more than 14 percent after exposure to water at about C., which polymer contains in the polymer molecule at least about 80 weight percent of acrylonitrile, any balance being another monoethylenioally unsaturated monomeric material that is copolymerizable with acrylonitrile, into an aquagel filamentary structure that contains between about 1 and 5 parts by Weight of water to each part by weight of dry polymer therein; washing said aquagel substantially free from residual salt and physically elongating said fiber by stretching it to an at least partially oriented condition; subjecting said aquagel fiber to intimate contact with (a) at least one alcohol selected from the group consisting of tertiary alcohols and benzyl alcohols having the respective formulae:
R COH and X 3 G Hz 0 H wherein each R in said tertiary alcohol is an independently selected alkyl radical that contains from 1 to about 4 7 carbon atoms with the limitation that the total number of carbon atoms in all three substituents is from 3 to 7; and wherein each X in said benzyl alcohol is selected from the group consisting of hydrogen, chlorine, bromine and al'kyl radicals containing from 1 to about 4 carbons and n has a whole number value from to 5, said alcohol being employed in sufiicient quantity to convert between about 5 and 25 mole percent of the nitrile groups in said acrylonitrile polymer to acrylamide substituents; and (b) an aqueous solution of a strong dissociated inorganic acid containing about 40 to 95 percent by weight of the acid and selected from the group consisting of sulfuric acid, hydrochloric acid, and their mixtures; maintaining said aquagel in contact with said acid solution at a temperature between about 0 and 110 C. until between about 5 and 25 mole percent of said nitrile groups in the acrylonitrile polymer are converted to acrylamide substituents; washing the treated aquagel with water until it is free of residualacid; and subsequently irreversibly drying said aquagel fiber to a synthetic characteristically hydrophobic textile fiber structure.
2. The method of claim 1, wherein said acrylonitrile polymer is polyacrylonitrile.
3. The method of claim 1, wherein said alcohol is tertiary-amyl alcohol.
4. The method of claim 1, wherein said alcohol is tertiary butyl alcohol.
5. The method of claim 1, wherein said alcohol is benzyl alcohol.
6. The method of claim 1, wherein said acid is an aqueous solution of sulfuric acid having a concentration of H of between about and percent by weight.
7. Themethod of claim 1, wherein said aquagel fiber is contacted with said alcohol and .said acid solution in respective sequential treating baths.
8. The method ofclaim 1, wherein said aquagel fiber is contacted with said alcohol and said acid solution in a single bath containing a mixture of the alcohol and the acid.
9. The method of claim 1, wherein said aquagel is maintained in contact with said acid at a temperature between about 20 and 30 C. for a period of time of at' least about 5 minutes until between about 8 and 20 mole percent of the nitrile groups in the recurring acrylonitrile;
units are converted to acrylamide substituents.
References Cited in the file of this patent UNITED STATES PATENTS

Claims (1)

1. METHOD OF PREPARING A DYE-RECEPTIVE AND HIGHLY SHRINKABLE SYNTHETIC ACRYLONITRILE POLYMER TEXTILE FIBER WHICH METHOD COMPRISES SALT SPINNING A FIBER-FORMING ACRYLONITRILE POLYMER THAT IS ADAPTED TO PROVIDE FIBERS WHICH DO NOT SHRINK MORE THAN 14 PERCENT AFTER EXPOSURE TO WATER AT ABOUT 100*C., WHICH POLYMER CONTAINS IN THE POLYMER MOLECULE AT LEAST ABOUT 80 WEIGHT PERCENT OF ACRYLONITRILE, ANY BALANCE BEING ANOTHER MONOETHYLENICALLY UNSATURATED MONOMERIC MATERIAL THAT IS COPOLYMERIZABLE WITH ACRYLONITRILE, INTO AN AQUAGEL FILAMENTARY STRUCTURE THAT CONTAINS BETWEEN ABOUT 1 AND 5 PARTS BY WEIGHT OF WATER TO EACH PART BY WEIGHT OF DRY POLYMER THEREIN, WASHING SAID AQUAGEL SUBSTANTIALLY FREE FROM RESIDUAL SALT AND PHYSICALLY ELONGATING SAID FIBER BY STRETCHING IT TO AN AT LEAST PARTIALLY ORIENTED CONDITION, SUBJECTING SAID AQUAGEL FIBER TO INTIMATE CONTACT WITH (A) AT LEAST ONE ALCOHOL SELECTED FROM THE GROUP CONSISTING OF TERTIARY ALCOHOLS AND BENZYL ALCOHOLS HAVING THE RESPECTIVE FORMULAE:
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3071791A (en) * 1961-01-19 1963-01-08 Eastman Kodak Co Control of static electrification by use of mixture brushes
US3088932A (en) * 1960-12-02 1963-05-07 Monsanto Chemicals Acrylonitrile polymer composition and stabilized with zinc oxalate, zinc acetate, or chromium acetate

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US1984417A (en) * 1929-07-25 1934-12-18 Ig Farbenindustrie Ag Production of artificial masses
US2431956A (en) * 1945-05-04 1947-12-02 Du Pont Dyeing articles composed of acrylonitrile polymers
US2579451A (en) * 1948-12-31 1951-12-18 Du Pont Polymeric materials
US2611929A (en) * 1951-06-18 1952-09-30 Chemstrand Corp Method of producing shaped articles from artificial or synthetic fiberor film-forming materials
US2645556A (en) * 1951-07-25 1953-07-14 Courtaulds Ltd Production of artificial filaments
CA519628A (en) * 1955-12-20 American Cyanamid Company Treatment of acrylonitrile polymerization products
US2776271A (en) * 1952-10-21 1957-01-01 Eastman Kodak Co Mixtures comprising acrylonitrile polymers containing alkenyl carbonamides and polyacrylonitrile
US2850477A (en) * 1952-11-10 1958-09-02 Chemstrand Corp Polymeric vinylcarbazole fiberforming compositions

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Publication number Priority date Publication date Assignee Title
CA519628A (en) * 1955-12-20 American Cyanamid Company Treatment of acrylonitrile polymerization products
US1984417A (en) * 1929-07-25 1934-12-18 Ig Farbenindustrie Ag Production of artificial masses
US2431956A (en) * 1945-05-04 1947-12-02 Du Pont Dyeing articles composed of acrylonitrile polymers
US2579451A (en) * 1948-12-31 1951-12-18 Du Pont Polymeric materials
US2611929A (en) * 1951-06-18 1952-09-30 Chemstrand Corp Method of producing shaped articles from artificial or synthetic fiberor film-forming materials
US2645556A (en) * 1951-07-25 1953-07-14 Courtaulds Ltd Production of artificial filaments
US2776271A (en) * 1952-10-21 1957-01-01 Eastman Kodak Co Mixtures comprising acrylonitrile polymers containing alkenyl carbonamides and polyacrylonitrile
US2850477A (en) * 1952-11-10 1958-09-02 Chemstrand Corp Polymeric vinylcarbazole fiberforming compositions

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3088932A (en) * 1960-12-02 1963-05-07 Monsanto Chemicals Acrylonitrile polymer composition and stabilized with zinc oxalate, zinc acetate, or chromium acetate
US3071791A (en) * 1961-01-19 1963-01-08 Eastman Kodak Co Control of static electrification by use of mixture brushes

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