Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
  • C08B16/00—Regeneration of cellulose
• • 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
  • D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
  • D01F2/06—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
  • D01F2/08—Composition of the spinning solution or the bath
  • D01F2/10—Addition to the spinning solution or spinning bath of substances which exert their effect equally well in either

Definitions

• This invention relates to the production of shaped bodies of regenerated cellulose from viscose and more particularly to filaments and fibers of regenerated cellulose from viscose.
• a suitable cellulosic material such as purified cotton linters, wood pulp, mixtures thereof, and the like is first converted to an alkali cellulose by treatment with a caustic soda solution and after shredding the treated cellulose material, it is allowed to age.
• the aged alkali cellulose is then converted to a xanthate by treatment with carbon disulfide.
• the cellulose xanthate is subsequently dissolved in a caustic soda solution in an amount calculated to provide a viscose of the desired cellulose and alkali content.
• the viscose solution is allowed to ripen and is subsequently extruded through a shaped orifice into a suitable coagulating and regenerating bath.
• the viscose solution is extruded through a spinneret into a coagulating and regenerating bath consisting of an aqueous acid solution containing zinc sulfate.
• the filament may subsequently be passed through a hot aqueous bath where it is stretched to improve its properties such as tensile strength.
• the filament may then be passed through a dilute aqueous solution of sulfuric acid and sodium sulfate to complete the regeneration of the cellulose, in case it is not completely regenerated upon leaving the stretching stage.
• the filament is subsequently subjected to washing, purification, bleaching, possibly other treating operations and drying, being collected either before or after these treatments.
• the filaments as formed by the conventional methods consist of a skin or outer shell portion and a core portion with a sharp line of demarcation between the two.
• the cross-section of the filaments exhibits a very irregular or crenulated exterior surface when even small amounts of zinc salts or certain other polyvalent metal salts are present in the spinning bath.
• the skin and core portions of the filament represent differences in structure and these different portions possess different swelling and staining characteristics, the latter permitting a ready identification of skin and core.
• the sharply irregular and crenulated surface structure has a relatively low abrasion resistance and readily picks up foreign particles such as dirt.
• the core portion posseses a relatively high tensile strength, it has a low abrasion resistance and a low flex-life, is subject to fibrillation and is relatively stiff.
• the alkylene oxide adduct utilized in the modification of the viscose may be an adduct of either the alpha or beta forms of N-fatty alkyl alanine.
• the fatty alkyl group or radical is a straight hydrocarbon chain containing from 6 to 24 carbon atoms and may be saturated or unsaturated.
• the radical may be obtained from the fatty acids derived from animal and vegetable fats and oils such as coconut oil, cottonseed oil, corn oil, soya bean oil, palm oils, peanut oil, tallow and the like and the hydrogenated fats and oils.
• the N-fatty alkyl alanine as utilized for the purposes of this invention may be a pure compound wherein a relatively pure fatty alkyl radical, such as a lauryl radical, is employed in preparing the adduct, or the N-fatty alkyl alanine mayconsist of a mixture of compounds where the fatty alkyl radicals are obtained from a mixture of fatty acids of a particular fat oroil such as coconut oil.
• the adducts may be prepared by reacting a N-fatty alkyl alanine, or a mixture of N-fatty alkyl alanines with an alkylene oxide or a polyoxyalkylene glycol.
• Adducts which are satisfactory for the purposes of this invention may be derived from capric, lauric, myristic, oleic, stearic acids and like acids or from a mixture of fatty acids such as obtained from coconut oil or other fat or oil.
• the compounds may be conveniently added to viscose in the form of solutions in alkali or in water.
• This invention contemplates the use of alkylene oxide adducts of N-fatty alkyl alanines having from about 8 to about 30 or more alkylene oxide units per molecule, preferably between about 12 and 20 alkylene oxide units per molecule of the N-fatty alkyl alanine. It is obvious that for all practical purposes considering cost, ease of preparation, commercial availability and solubility in water and in alkali solutions, the ethylene oxide adducts are preferred. For purposes of illustration only, the invention is described by reference to'the ethylene oxide adducts but it is to be understood that other alkylene oxide adducts such as propylene oxide adducts are equally satisfactory so long as they possess the required solubility.
• the adduct must have suflicient solubility to permit a minimum amount of the adduct to be dissolved in the viscose.
• Commercial materials of this type such as the substance marketed as Good-Rite CEA are entirely satisfactory.
• This substance is an ethylene oxide adduct of a mixture of N-fatty alkyl alanines wherein the fatty alkyl radicals are obtained from coconut oil and have an average of about 15 ethylene oxide units per molecule of the N-fa'tty alkyl alanine.
• the amountof the adduct or modifier which is incorporated in the viscose must be at least about 0.5% by weight of the cellulose in the viscose and may vary up to about 4%, preferably, the amount varies from 0.5% to 2.5%. V tion of products consisting entirely of skin and greater amounts affect adversely the physical properties of the. products. Amounts within the preferred range are most; effective in enhancing the characteristics and properties.
• the adduct may be added at any desired stage in the production of the viscose such as in the preparation of the refined wood pulp for the manufacture of viscose, before or during the shredding of the alkali cel-- lulose, to the xanthated cellulose while it is being dis solved in the caustic solution or to the viscose solution before or after filtration.
• the adduct is preferably added Lesser amounts do not result in the produce,
• the viscose may contain from about 6% to about 8% cellulose, the particular source of the cellulose being selected for the ultimate use of the regenerated cellulose product.
• the caustic soda content may be from about 4% to about 8%.
• the carbon disulfide content may be from about 30% to about 50% based upon the weight of the cellulose.
• the modified viscose that is, a viscose containing. the small amount of an alkylene oxide adduct of a N-fatty alkyl alanine may have a salt test above about 7 and preferably above about 9 at the time of spinning or extrusion.
• the composition of the spinning bath be maintained within a well defined range.
• the presence of the .alkylene oxide adduct in the viscose combined with these limited spinning baths results in the. production of yarns of improved properties such as high tenacity, high abrasion resistance, high fatigue resistance and consisting of filaments composed entirely of skin.
• the spinning bath is a low acid-high zinc spinning bath containing from about 10% to about 25% sodium sulfate and from about 3% to about 15% zinc sulfate, preferably from 15% to 22% sodium sulfate and from 4% to 9% zinc sulfate.
• Other metal sulfates such as iron, manganese, nickel and the like may be present and may replace some of the zinc sulfate.
• the temperature of the spinning bath may vary from about 25 C. to about 80 C., preferably between about 45 C. and about 70 C.
• the temperature of the spinning bath is not critical, however, as is well known in the conventional practice in the art, certain of the physical properties such as tensile strength vary directly with the temperature of the spinning bath.
• the spinning bath is preferably maintained at a temperature between about 55 C. and 65 C. so as to obtain the desired high tensile strength.
• the acid content of the spinning bath is balanced against the composition of the viscose.
• the lower limit of the acid concentration is just above the slubbing point, that is, the concentration at which small slubs of uncoagulated viscose appear in the strand as it leaves the spinning bath.
• the acid concentration of the spinning bath is generally maintained about 0.4% to 0.5% above the slubbing point.
• the acidconcentration of the spinning bath must be maintained above the slubbing point and below the point at which the neutralization of the caustic of the viscose is sufficiently rapid to form a filament having a skin and core.
• the acid concentration of the spinning baths which are satisfactory for the production of the all skin products from a 7% cellulose, 6% caustic-viscose and containing the alkylene oxide adducts lies between about and about 8%.
• the acid concentration may be increased as the amount of the derivative is increased and also as the salt test of the viscose is increased.
• the acid concentration based upon the amount of adduct and the concentration of caustic in the viscose.
• the adducts in the viscose retards the coagulation and, therefore, the amount of adduct employed must be reduced at high spinning speeds.
• the adduct is employed in amounts within the lower portion of the range, for example, about 0.6% to 0.75%.
• the extruded viscose must, of course, be immersed or maintained in the spinning bath for a period sufiicient to effect relatively complete coagulation of the viscose, that is, the coagulation must be sufiicient so that the filaments will not adhere to each other as they are brought together and withdrawn from the bath.
• the filaments are preferably stretched after removal from the initial coagulating and regenerating bath.
• the filaments may be passed through a hot aqueous bath which may consist of hot water or a dilute acid solution and may be stretched from about 70% to about 120%, preferably between and Yarns for other textile purposes may be stretched as low as 20%.
• the precise amount of stretching will be dependent upon the desired tenacity and other properties and the specific type of product being produced.
• the filaments may be stretched in air. It is to be understood that the invention is not restricted to the production of filaments and yarns but it is also applicable to other shaped bodies such as sheets, films, tubes and the like.
• the filaments may then be passed through a final regenerating bath which may contain from about 1% to about 5% sulfuric acid and from about 1% to about 5% sodium sulfate with or without small amounts of zinc sulfate if regeneration has not previously been completed.
• the treatment following the final regenerating bath, or the stretching operation where regeneration has been completed may consist of a washing step, a desulfurizing step, the application of a finishing or plasticizing material and drying before or after collecting, or may include other desired and conventional steps such as bleaching and the like.
• the treatment after regeneration will be dictated by the specific type of shaped body and the proposed use thereof.
• Regenerated cellulose filaments prepared from viscose containing the small amounts of the alkylene oxide adducts and spun in the spinning baths of limited acid content have a smooth or non-crenulated surface and consist substantially entirely of skin. Because of the uniformity of structure throughout the filament, the swelling and staining characteristics are uniform throughout the cross-section of the filament. Filaments produced pursuant to this invention and consisting entirely of skin have a high toughness and a greater flexing life than filaments as produced according to prior methods which may be attributed by the uniformity in skin structure throughout the filament.
• the invention may be illustrated by reference to the preparation of regenerated cellulose filaments from a viscose containing about 7.4% cellulose, about 6.3% caustic soda, and having a total carbon disulfide content of about 41% based on the weight of the cellulose.
• the viscose solutions were prepared by xanthating alkali cellulose by the introduction of 36% carbon disulfide based on the weight of the cellulose and churning for about 2% hours. The cellulose xanthate was then dissolved in caustic soda solution. An additional 5% carbon disulfide was then added to the mixer and the mass mixed for about one hour. The desired amount of the ethylene oxide adduct of N-fatty alkyl alanine was added to the solution and mixed for about /2 hour. The viscose was then allowed to ripen for about 30 hours at 18 C.
• Example 1 Approximately 1% (based on the weight of the cellulose) of an ethylene oxide adduct of N-fatty alkyl alanine (fatty alkyl groups from coconut oil) known as Good- Rite CEA was added to and incorporated in the viscose as described above.
• the viscose employed in the spinning of filaments had a salt test of 9.4.
• the viscose was extruded through a spinneret to form a 208 denier, 120 filament yarn at a rate of about 22 meters per minute.
• the coagulating and regenerating bath was maintained at a temperature of about 60 C. and contained 7.8% sulfuric acid, 8% zinc sulfate and 17% sodium sulfate.
• the yarn was stretched about 82% while passing through a hot water bath at 95 C. The yarn was collected in a spinning box, washed free of acids and salts and dried.
• the individual filaments have a smooth, non-crenulated exterior surface and consist entirely of skin, no core being detectable at high magnification (e.g. 1500X).
• Other physical properties are set forth in the table which follows the examples.
• Example 2 To a viscose as described above, there was added 2% of the same ethylene oxide adduct (Good-Rite CEA). The viscose had a salt test of 9.4 and was spun into a 202 denier, 120 filament yarn by extrusion into a spinning bath containing 7.8% sulfuric acid, 8% zinc sulfate and 17% sodium sulfate. The bath was maintained at 60 C. and the extrusion rate was about 43 meters per minute. The filaments were subsequently passed through a hot water bath at 95 C. and stretched about 74%. The yarn was collected in a spinning box, washed free of acids and salts and dried.
• Good-Rite CEA ethylene oxide adduct
• control filaments were readily distinguishable from control filaments in that they have a smooth, noncrenulated surface and consist entirely of skin while the control filaments have a very irregular and serrated surface and consist of about skin and the balance core with a sharp line of demarcation between the skin and core.
• Other physical properties are set forth in the table which follows the examples.
• the bath was maintained at a temperature of 60 C.
• the extrusion rate was about 22 meters per minute.
• the water bath was maintained at about 95 C. and the filaments were stretched approximately 82% while passing through the hot water.
• the yarn was collected in a spinning box, washed free of acid and salts and dried.
• control filaments prepared from viscose containing no modifier in that they have a smooth, non-crenulated surface and consist entirely of skin.
• Control filaments have a very irregular and serrated surface and consist of about 85 skin and the balance core with a sharp line of demarcation between the skin and core.
• Other physical properties are set forth in the table which follows the examples.
• Example 4 As a control for the foregoing examples, a viscose solution, prepared as described above, having a salt test of 9.7 was spun into a 210 denier, 120 filament yarn by extrusion into a bath containing 7.5% sulfuric acid, 8% zinc sulfate and 19% sodium sulfate. The bath was maintained at a temperature of about 60 C. The extrusion rate was about 22 meters per minute. The water bath was maintained at a temperature of about C. and the filaments were stretched 82% while passing through the hot water. The yarn was collected in a spinning box, washed free of acid and salts and dried.
• the individual filaments have a very irregular and serrated surface and consist of about 85 skin and the balance core with a sharp line of demarcation between the skin and the core. Other characteristics are set forth in the table which follows:
• tenacity and elongation are the only properties set forth, they have been chosen because of the ease and simplicity with which such properties may be determined. In some instances, products made in accordance with this invention do not exhibit improvements in tenacity and elongation, however, the products consist of a smooth-surfaced, all skin structure and possess improved abrasion resistance, flex-life and other properties as disclosed hereinbefore.
• the swelling amounting to from about 45% to about 60%.
• the alkylene oxide adducts may be added to any desired viscose such as those normally used in industry, the specific Viscose composition set forth above being merely for illustrative purposes.
• the adducts may be added at any desired stage in the production of the viscose and may be present in the cellulosic raw material although it may be necessary to adjust the amount present to produce a viscose having the proper proportions of the adduct at the time of spinning.
• the term skin is employed to designate that portion of regenerated cellulose filaments which is permanently stained or dyed by the following procedure: A microtome section of one or more of the filaments mounted in a wax block is taken and mounted on a slide with Meyers albumin fixative. After dewaxing in xylene, the section is placed in successive baths of 60% and 30% alcohol for a few moments each, and it is then stained in 2% aqueous solution of Victoria Blue BS cone. (General Dyestuffs Corp.) for 1 to 2 hours. At this point, the entire section is blue.
• the dye By rinsing the section first in distilled water and then in one or more baths composed of 10% water and 90% dioxane for a period varying from 5 to 30 minutes depending on the particular filament, the dye is entirely removed from the core, leaving it restricted to the skin areas.
• a viscose spinning solution containing a small amount of a modifier selected from the group consisting of alkylene oxide adducts of N-fatty alkyl alanines and mixtures thereof, the fatty alkyl group being a straight hydrocarbon chain containing from 6 to 24 carbon atoms, the alkylene oxide being selected from the group consisting of ethylene oxide and propylene oxide, the adducts containing at least 8 alkylene oxide units per molecule of N-fatty alkyl alanine, said small amount of the; modifier being a quantity sufficient to impart a smooth, noncrenulated surface and a substantially all skin structure to products formed by spinning the viscose at a sodium chloride salt test of at least 7 into an aqueous bath containing from 15% to 22% sodium sulfate, from 4% to 9% zinc sulfate and sulfuric acid in an amount not exceeding 8.5%, but the quantity being insufficient to adversely'affect the physical properties of such products.
• a modifier selected from the group
• a viscose spinning solution containing from about 0.5% to about 4%, based on the Weight of the cellulose in theviscose of a modifier selected from the group consisting of alkylene oxide adducts of N-fatty alkyl alanines and mixtures thereof, the fatty alkyl group being a straight hydrocarbon chain containing from 6 to 24 carbon atoms, the alkylene oxide being selected from the group consisting of ethylene oxide and propylene oxide, the adducts containing at least about 8 alkylene oxide units per molecule of N-fatty alkyl alanine.
• a modifier selected from the group consisting of alkylene oxide adducts of N-fatty alkyl alanines and mixtures thereof, the fatty alkyl group being a straight hydrocarbon chain containing from 6 to 24 carbon atoms, the alkylene oxide being selected from the group consisting of ethylene oxide and propylene oxide, the adducts containing at least about 8 alkylene oxide units per molecule of N

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• 0
  • NL NL201022D patent/NL201022A/xx unknown
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  • BE BE543402D patent/BE543402A/xx unknown
• 1955
  • 1955-09-15 GB GB26408/55A patent/GB787486A/en not_active Expired
  • 1955-12-05 FR FR1144224D patent/FR1144224A/fr not_active Expired
  • 1955-12-14 CH CH345713D patent/CH345713A/fr unknown
• 1958
  • 1958-11-25 US US776204A patent/US2961329A/en not_active Expired - Lifetime

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