US2506710A - Production of high tenacity filamentary materials - Google Patents
Production of high tenacity filamentary materials Download PDFInfo
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- US2506710A US2506710A US720070A US72007047A US2506710A US 2506710 A US2506710 A US 2506710A US 720070 A US720070 A US 720070A US 72007047 A US72007047 A US 72007047A US 2506710 A US2506710 A US 2506710A
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- United States
- Prior art keywords
- yarn
- cake
- cellulose
- yarns
- saponifying
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- 239000000463 material Substances 0.000 title description 11
- 238000004519 manufacturing process Methods 0.000 title description 6
- 239000004744 fabric Substances 0.000 description 20
- 229920002678 cellulose Polymers 0.000 description 17
- 239000001913 cellulose Substances 0.000 description 16
- 239000004627 regenerated cellulose Substances 0.000 description 16
- 238000009987 spinning Methods 0.000 description 16
- 239000003795 chemical substances by application Substances 0.000 description 15
- 238000000034 method Methods 0.000 description 15
- -1 organic acid ester Chemical class 0.000 description 14
- 229920002301 cellulose acetate Polymers 0.000 description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 238000007127 saponification reaction Methods 0.000 description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 238000004804 winding Methods 0.000 description 9
- 239000007864 aqueous solution Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 3
- 238000012937 correction Methods 0.000 description 3
- 239000001632 sodium acetate Substances 0.000 description 3
- 235000017281 sodium acetate Nutrition 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- 230000001476 alcoholic effect Effects 0.000 description 2
- SWXVUIWOUIDPGS-UHFFFAOYSA-N diacetone alcohol Chemical compound CC(=O)CC(C)(C)O SWXVUIWOUIDPGS-UHFFFAOYSA-N 0.000 description 2
- 238000000578 dry spinning Methods 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 2
- UTACNSITJSJFHA-UHFFFAOYSA-N 1,1,1,3-tetrachloropropane Chemical compound ClCCC(Cl)(Cl)Cl UTACNSITJSJFHA-UHFFFAOYSA-N 0.000 description 1
- HXDLWJWIAHWIKI-UHFFFAOYSA-N 2-hydroxyethyl acetate Chemical compound CC(=O)OCCO HXDLWJWIAHWIKI-UHFFFAOYSA-N 0.000 description 1
- XLLIQLLCWZCATF-UHFFFAOYSA-N 2-methoxyethyl acetate Chemical compound COCCOC(C)=O XLLIQLLCWZCATF-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 101710085461 Alpha-tubulin N-acetyltransferase 1 Proteins 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 241001589086 Bellapiscis medius Species 0.000 description 1
- 229920008347 Cellulose acetate propionate Polymers 0.000 description 1
- DQEFEBPAPFSJLV-UHFFFAOYSA-N Cellulose propionate Chemical compound CCC(=O)OCC1OC(OC(=O)CC)C(OC(=O)CC)C(OC(=O)CC)C1OC1C(OC(=O)CC)C(OC(=O)CC)C(OC(=O)CC)C(COC(=O)CC)O1 DQEFEBPAPFSJLV-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- HKQOBOMRSSHSTC-UHFFFAOYSA-N cellulose acetate Chemical compound OC1C(O)C(O)C(CO)OC1OC1C(CO)OC(O)C(O)C1O.CC(=O)OCC1OC(OC(C)=O)C(OC(C)=O)C(OC(C)=O)C1OC1C(OC(C)=O)C(OC(C)=O)C(OC(C)=O)C(COC(C)=O)O1.CCC(=O)OCC1OC(OC(=O)CC)C(OC(=O)CC)C(OC(=O)CC)C1OC1C(OC(=O)CC)C(OC(=O)CC)C(OC(=O)CC)C(COC(=O)CC)O1 HKQOBOMRSSHSTC-UHFFFAOYSA-N 0.000 description 1
- 229920006217 cellulose acetate butyrate Polymers 0.000 description 1
- 229920001727 cellulose butyrate Polymers 0.000 description 1
- 229920006218 cellulose propionate Polymers 0.000 description 1
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 150000004292 cyclic ethers Chemical class 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 150000003567 thiocyanates Chemical class 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000002166 wet spinning Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
- D06M11/32—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond
- D06M11/36—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond with oxides, hydroxides or mixed oxides; with salts derived from anions with an amphoteric element-oxygen bond
- D06M11/38—Oxides or hydroxides of elements of Groups 1 or 11 of the Periodic Table
- D06M11/385—Saponification of cellulose-acetate
-
- 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
- D01D10/04—Supporting filaments or the like during their treatment
- D01D10/0418—Supporting filaments or the like during their treatment as cakes or similar coreless thread packages
-
- 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
- D01F2/24—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from cellulose derivatives
- D01F2/28—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from cellulose derivatives from organic cellulose esters or ethers, e.g. cellulose acetate
Definitions
- This invention relates to the production of high tenacity filamentary materials, and relates more particularly to an improved process for the saponification of stretched filamentary materials, such as films, threads and yarns (hereinafter referred to as yarns) having a basis of an organic acid ester of cellulose whereby high tenacity regenerated cellulose yarns are obtained.
- High tenacity regenerated cellulose yarns of high degree of strength have been obtained by stretching filamentary materials having a basis of cellulose acetate or other organic acid ester of'cellulose from 100 to 2000% of their original length, and then subjecting such stretched yarn to the action of a basic saponifying agent to split off the combined acyl groups.
- the saponification of the stretched yarns has been usually efiected after the stretched yarns were backwound from the packages, on which they were taken up after the stretching operation, onto a perforated bobbin.
- a plurality of stainless steel bobbins of yarn were then placed in a suitable enclosed vessel and the saponifying liquid circulated through the windings of yarn on the bobbin by supplying the saponifying liquid thereto under moderate pressure until the saponification of the yarn on the bobbins was completed.
- This method of saponifying yarn was not wholly satisfactory both from the standpoint of economy and also of manipulation.
- the bobbins must preferably be made of stainless steel which made them heavy and expensive.
- the bobbins were not only hard to handle but also could not be made desirably large and only a limited amount of yarn could be placed thereon. Moreover, the yarn had to be wound onto the bobbins with extraordinary care otherwise the saponiiication was effected non-uniformly. Again, since the saponification causes shrinkage of the yarn in diameter by loss of combined acetic acid, often up to 35%, a soft package results making for difficulty in unwinding the same.
- the yarn may first be wound into cake form and the sock placed over said cake after it is removed from the arbor on which it is formed.
- the materials saponified in accordance with my invention may comprise yarns of cellulose acetate or other organic acid ester of cellulose which have been subjected to stretching, in one or a plurality of stages, and taken up on a ring bobbin with a twist of about turn per inch.
- the stretching may be effected in suitable stretching apparatus with steam or hot water and may be facilitated by means of solvents, latent solvents or swelling agents for the cellulose acetate or other cellulose esters, for example aqueous solutions of thiocyanates, such as those of the alkali metals, ammonium or alkaline earth metals, or aqueous solutions of zinc chloride; acetic acid, formic acid, lactic acid, diacetone alcohol, acetone, the ethers and esters of ether-esters of olefine and polyoleflne glycols, for instance glycol mono-acetate, methyl glycol mono-acetate, the acetins, diozane and its homoiogues and substitution products, methylene ethylene ether and its homologues and substitution products and similar cyclic ethers, dichlorethylene, methylene chloride and the like.
- solvents, latent solvents or swelling agents for the cellulose acetate or other cellulose esters for example aqueous
- Such organic solvents, latent solvents or swelling agents may be applied in conjunction with any suitable diluent, for example, water, benzene and its homologues, petroleum fractions or other aliphatic hydrocarbons and chlorinated hydrocarbons, e. g. carbon tetrachloride, which have precipitating action or at least little or no solvent action upon the cellulose acetate or other organic acid ester of cellulose treated.
- suitable diluent for example, water, benzene and its homologues, petroleum fractions or other aliphatic hydrocarbons and chlorinated hydrocarbons, e. g. carbon tetrachloride, which have precipitating action or at least little or no solvent action upon the cellulose acetate or other organic acid ester of cellulose treated.
- the stretching for the purposes of the present invention should involve a very substantial extension of the filaments, yarns or other products, and in particular extensions of the order of 100, 200, 300, 500, 1000% or more. The stretching may be applied either to we
- the yarn may be stretched considerably during its formation.
- this involves a softening treatment during the dry spinning process so as to enable substantial stretch to be imparted to the materials, while in the case of wet spinning the nature of the coagulatin bath or of the spinning solution may be such' that a very considerable stretch may be imparted to the materials during their actual formation.
- the stretching of the materials shouldbe such as tively high tenacity, preferably in excess of 2 to 2.5 grams per denier, .and may attain values of 3 to 4 grams per denier or more.
- the stretched yarns are then up-twisted into cake form by means of any suitable cake twisting machine such as, for example, a convention twistercheeser adapted to feed the yarn at suitable and controlled tension on which the cake may be formed with a traverse wind at the beginning of the cake of l to 1 /8.
- a suitable cake twisting machine such as, for example, a convention twistercheeser adapted to feed the yarn at suitable and controlled tension on which the cake may be formed with a traverse wind at the beginning of the cake of l to 1 /8.
- a suitable cake twisting machine such as, for example, a convention twistercheeser adapted to feed the yarn at suitable and controlled tension on which the cake may be formed with a traverse wind at the beginning of the cake of l to 1 /8.
- the stretched y rn from the spinning bobbin on which it was taken up during the stretching operation is up-twisted onto a suitable arbor over which a fabric sock i first drawn, the yarn being cross-wound at
- the cake is preferably wound on the fabric sock covered arbor to an outside diameter of about 7 inches with a wall thickness of about 1 inches. After the winding of the cake is removed from the arbor, the sock is wrapped completely around the same and a suitable expander inserted in the yarn cake to maintain the shape thereof. The expander is removed during the subsequent saponification operation and reinserted thereafter remaining inside the cake throughout the remaining operations.
- the use of the fabric sock offers many advantages; thus, the handling of the cake is effected without damage to the yarn windings, the saponification and subsequent operations are to impart thereto a rela-' cifected in a more uniform manner resulting in a more uniform product, and the fabric sock surrounding the cake also acts as a filtering medium preventing the passage therethrough of any extraneous substances which may be present in the treating liquids.
- the sock may be made of any other suitable material such as, for example, circular knit cotton fabric or a suitably treated paper.
- the regenerated cellulose yarns produced are found to be more uniform, to have higher dry and wet tenacities, to have fewer broken ends and to be cleaner than the regenerated cellulose yarns formed by prior processes of saponifying cellulose acetate or other organic acid esters of cellulose.
- the saponifying agent may be in the form of an aqueous, alcoholic or aqueous/alcoholic solution of any suitable basic agent, and may be sprayed onto the stretched cellulose acetate or other organic acid'ester of cellulose yarns in any convenient manner.
- the saponifying agent may be inorganic in nature such as, for example, sodium hydroxide or potassium hydroxide.
- Organic saponifying agents such as, for example, methyl amine, ethylene diamlne or triethanolamine, may also be employed. It is preferred that the saponifying solution also contain from about 6 to 10% by weight of sodium acetate which assists materially in preventing degradation of the yarn undergoing saponiflcation.
- I employ an aqueous solution of sodium hydroxide as the saponifying agent and in concentrations of 0.1 to 5% by weight.
- I have obtained highly desirable results by employing a 0.6% aqueous solution of sodium hydroxide containing 8 to 10% of sodium acetate as the saponifying medium and supplying this medium to the spinning bucket at a temperature from 140 to 180 F. and at a rate of 4 gallons per minute. While the temperature of the saponiflcation medium may range from 20 to C., I have found that optimum results are obtained when the temperature of the saponiflcation medium is as stated, namely from to 180 F.
- the saponiflcation medium is introduced in the center of the cake in the spinning bucket and centrifugally distributed and dispelled throughout the cake.
- the spinning bucket is preferably rotated at the rate of about 730 R. P. M.
- the cake of yarn is subjected to the saponiflcation treatment rotating spinning bucket for about 2 hours after which it is washed while still in the spinning bucket and finally dried for 24 hours at a temperature of about to F.
- the cake is then placed on a wood cake holder and wound into any desired package form employing conventional textile apparatus.
- Fig. l is a view, partly in section, showing a centrifuge in which the saponiflcation of the yarn cake is effected
- Fig. 2 is a perspective view of the yarn cake surrounding the fabric sock as it is taken ed the arbor on which the yarn cake is wound, and
- Fig. 3 is a cross-sectional view of the yarn cake completely enclosed by the fabric sock.
- the reference numeral t indicates a tank for holding the saponifying agent which is fed through conduit 5 to a pump 6 adapted to supply the saponifying agent at the desired rate to a centrifuge generally indicated by reference numeral 1 through a conduit 8.
- the lower end of conduit 8 is perforated and forms a distributing header 9 extending within the centrifuge.
- the centrifuge 1 comprises a spinning pump I l to which is attached a shaft i2 extending through the bottom of the outer housing i3 of the contrifuge.
- the shaft i2 is adapted to be rotated at the desired speed by any suitable means.
- the spinning bucket is provided with openings [6 in the centrifugal wall thereof in which the saponifying agent is removed as it passes through the yarn cake i5.
- the bottom of outer casing i3 is provided with a suitable drain or outlet I 6 which, if desired, may be connected to a pipe I! for returning the saponifying agent to the tank 4 for recycling the same.
- the yarn cake i 5 which was wound on an arbor with a fabric sock i8 has the sock completely covering the same with the ends overlapping, as shown in is in Fig. 3, before it is placed in the spinning bucket ii of the centrifuge.
- the yarn cake is placed in the spinning bucket in such a manner that the header 9 is substantially in the middle of the opening in said yarn cake.
- annular plate 2! is placed upon the yarn cake, remaining thereon throughout the saponiflcation process.
- the weight of the annular plate fl is such that it will cause contraction in the yarn cake as the saponification of said yarn cake proceeds causing the denier oi the yarn forming the cake to decrease.
- Example A filament, 32.5 denier cellulose acetate yarn which has been given a stretch of 900% is backwound with a twist of 2%; turns per inch, from the bobbins on which the yarn was taken up with a twist of turn per inch during the stretching operation, in the form of a cake on to the 'aibor of a Whitin twister cheeser, the arbor being slightly tapered and being first covered with a fabric sock.
- the yarn cake is wound on the fabric sock to a weight of 1.7 pounds with a traverse wind of 1 to 1% at the start of the cake.
- the yarn cake and the fabric sock are then removed together from the arbor, the ends of the sock are then turned on the outer windings of the yarn cake so as to cover the yarn cake completely and an expander is inserted in the covered yarn cake to maintain the shape thereof.
- the fabric sock-covered yarn cake after the expander is removed therefrom, is placed in a winning bucket and a centrifuge and an annular plate of appreciable weight is seated thereon.
- Saponifying liquid comprising a 0.6% aqueous solution is forced into a spinning bucket at a speed of 730 R. P. M. at the rate of 4 gallons per minute for 2 hours, the temperature of the saponifying liquid being 140 F.
- the saponified yarn cake is then washed for 30 minutes with softener-heated water at 140 F. and dried for 24 hours at 150 F.
- the expander is again inserted in the dried yarn cake and yarn of the cake is then wound into a cone.
- the regenerated cellulose yarn produced by this economical method is of better quality with respect to uniformity of saponification than the regenerated cellulose produced by saponifying stretched yarn by the bobbin method.
- the regenerated cellulose yarn produced in accordance with my process has a dry tenacity of 7.12, a dry elongation of 6.3, a wet tenacity of 6.20 and wet elongation of 6.5.
- the cellulose acetate yarns stretched and saponified in accordance with the process of this invention to yield regenerated cellulose of improved quality may be prepared by extruding a solution of cellulose'acetate dissolved in a suitable solvent through a plurality of orifices into an evaporative medium as in the dry method of spinning or into a coagulating or precipitating liquid medium as in the wet method of spinning.
- the filaments so formed are associated together to form the desired m-ulti-fllament yarn which are first stretched and then saponified.
- organic acid esters of cellulose may be employed for preparing regenerated cellulose yarns of improved tenacity.
- Such other organic acid esters of cellulose may be cellulose propionate, cellulose butyrate and mixed esters of cellulose, such as cellulose acetatepropionate and cellulose acetate-butyrate.
- the cellulose acetate or other organic acid ester of cellulose employed may be of any degree of esterlfication, for example, where cellulose acetate is employed it may have an acetyl value of from 40 to 62.5%, calculated as acetic acid.
- a process for preparing regenerated cellulose yarn of increased tenacity the steps of winding stretched yarn having a basis of an organic acid' ester of cellulose into cake form on a fabric stock while inserting a twist in said stretched yarn, completely covering said yarn cake with said fabric sock, placing said fabric covered yarn cake in a vessel rotating at a speed of 730 R. P. M., feeding a saponifylng medium comprising a 0.6% aqueous solution of sodium hydroxide, containing 8 to 10% of sodium acetate, at a temperature of F. into the rotating vessel at a rate of 4 gallons per minute to convert said organic acid ester of cellulose yarn into regenerated cellulose yarn, and winding said regenerated cellulose yarn from cake form into another form of yarn package.
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Artificial Filaments (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
Description
May 9, 1950 c. DREYFUS 2,506,710
PRODUCTION OF HIGH TENACITY FILAMENTARY MATERIALS Filed Jan. 3, 1947 I N VEN TOR.
E 1g: 2, CAMILLE DREYFUS,
AT TO RNE Y3 Fatentecfi May h,
TAT 1..
PRODUCTION OF HIGH TENACITY FILAMENTARY MATERIALS Camille Dreyfus, New York, N. Y. Application January 3, 1947, Serial No. 720,070
1 Claim.
This invention relates to the production of high tenacity filamentary materials, and relates more particularly to an improved process for the saponification of stretched filamentary materials, such as films, threads and yarns (hereinafter referred to as yarns) having a basis of an organic acid ester of cellulose whereby high tenacity regenerated cellulose yarns are obtained.
High tenacity regenerated cellulose yarns of high degree of strength have been obtained by stretching filamentary materials having a basis of cellulose acetate or other organic acid ester of'cellulose from 100 to 2000% of their original length, and then subjecting such stretched yarn to the action of a basic saponifying agent to split off the combined acyl groups.
The saponification of the stretched yarns has been usually efiected after the stretched yarns were backwound from the packages, on which they were taken up after the stretching operation, onto a perforated bobbin. A plurality of stainless steel bobbins of yarn were then placed in a suitable enclosed vessel and the saponifying liquid circulated through the windings of yarn on the bobbin by supplying the saponifying liquid thereto under moderate pressure until the saponification of the yarn on the bobbins was completed. This method of saponifying yarn was not wholly satisfactory both from the standpoint of economy and also of manipulation. Thus, the bobbins must preferably be made of stainless steel which made them heavy and expensive. Because of their weight, the bobbins were not only hard to handle but also could not be made desirably large and only a limited amount of yarn could be placed thereon. Moreover, the yarn had to be wound onto the bobbins with extraordinary care otherwise the saponiiication was effected non-uniformly. Again, since the saponification causes shrinkage of the yarn in diameter by loss of combined acetic acid, often up to 35%, a soft package results making for difficulty in unwinding the same.
Heretofore, the saponification of yarn was also eiiected while the yarn was in the form of a hank. Hanking, however, is a relatively expensive operation and the manipulating of hanks must be done with great care in order to avoid damage to the yarn. Moreover, the backwinding of hanks is a delicate operation and consumes much labor since tangling the yarn in such yarn packages is very easily efiected.
It is, accordingly, an important object of this invention to provide an improved process for saponifying stretched yarns having a basis of 2 cellulose acetate or other organic acid ester of cellulose which will be free from the foregoing and other disadvantages, and which will produce highly satisfactory high tenacity regenerated cellulose yarn emciently and economically.
Another object of this invention is the provision of an improved process for the saponiflcation of high tenacity stretched yarns having a basis of an organic acid ester of cellulose, where in most of the winding and backwinding of bob= bins is eliminated.
Other obiectsand advantages of this invention will appear from the following detailed descrip-= tion.
I have found that highly satisfactory high tenacity regenerated cellulose yarns may be pro= duced from stretched yarns having a basis of cellulose acetate or other organic acid ester of cellulose by a process involving a twist-winding of the stretched yarns onto a suitable arbor cov-= ered with a fabric socl: to form a cake, wrapping the fabric sock completely around the finished cake, removing the cake of yarn from the arbor, saponifying the cake of yarn while covered with the fabric sock, washing and drying the cake of yarn, and then winding the stretched and saponified yarn into the form of the desired ultimate package. It is to be understood, however, that the yarn may first be wound into cake form and the sock placed over said cake after it is removed from the arbor on which it is formed. The regenerated cellulose yarn produced in accordance with my invention is not only more uniform than the products obtained in accordance with prior processes but also has an appreciably higher tenacity. Moreover, there are produced longer lengths of knotless yarn, for the reasons, that larger pack= ages may be processed.
The materials saponified in accordance with my invention may comprise yarns of cellulose acetate or other organic acid ester of cellulose which have been subjected to stretching, in one or a plurality of stages, and taken up on a ring bobbin with a twist of about turn per inch. The stretching may be effected in suitable stretching apparatus with steam or hot water and may be facilitated by means of solvents, latent solvents or swelling agents for the cellulose acetate or other cellulose esters, for example aqueous solutions of thiocyanates, such as those of the alkali metals, ammonium or alkaline earth metals, or aqueous solutions of zinc chloride; acetic acid, formic acid, lactic acid, diacetone alcohol, acetone, the ethers and esters of ether-esters of olefine and polyoleflne glycols, for instance glycol mono-acetate, methyl glycol mono-acetate, the acetins, diozane and its homoiogues and substitution products, methylene ethylene ether and its homologues and substitution products and similar cyclic ethers, dichlorethylene, methylene chloride and the like. Such organic solvents, latent solvents or swelling agents may be applied in conjunction with any suitable diluent, for example, water, benzene and its homologues, petroleum fractions or other aliphatic hydrocarbons and chlorinated hydrocarbons, e. g. carbon tetrachloride, which have precipitating action or at least little or no solvent action upon the cellulose acetate or other organic acid ester of cellulose treated. The stretching for the purposes of the present invention should involve a very substantial extension of the filaments, yarns or other products, and in particular extensions of the order of 100, 200, 300, 500, 1000% or more. The stretching may be applied either to wet or dry spun yarns. Instead of or in addition to stretching the yarn after its formation, either continuously or discontinuously with its production, the yarn may be stretched considerably during its formation. In dry spinning operations, this involves a softening treatment during the dry spinning process so as to enable substantial stretch to be imparted to the materials, while in the case of wet spinning the nature of the coagulatin bath or of the spinning solution may be such' that a very considerable stretch may be imparted to the materials during their actual formation. In general, the stretching of the materials, either during, continuously with or after their formation, shouldbe such as tively high tenacity, preferably in excess of 2 to 2.5 grams per denier, .and may attain values of 3 to 4 grams per denier or more. The advantage of stretching to a considerable extent so as to obtain such high tenacities will be appreciated from the fact referred to above that the higher the tenacity of the stretched yarn the greater the increase in tenacity as a result of saponification treatment.
In accordance with my invention, the stretched yarns are then up-twisted into cake form by means of any suitable cake twisting machine such as, for example, a convention twistercheeser adapted to feed the yarn at suitable and controlled tension on which the cake may be formed with a traverse wind at the beginning of the cake of l to 1 /8. Thus, the stretched y rn from the spinning bobbin on which it was taken up during the stretching operation is up-twisted onto a suitable arbor over which a fabric sock i first drawn, the yarn being cross-wound at the desired density over the fabric sock. The yarn cake is preferably wound on a plastic arbor with an outside diameter of about 5 inches and which is slightly tapered to facilitate removal of the cake therefrom. The cake is preferably wound on the fabric sock covered arbor to an outside diameter of about 7 inches with a wall thickness of about 1 inches. After the winding of the cake is removed from the arbor, the sock is wrapped completely around the same and a suitable expander inserted in the yarn cake to maintain the shape thereof. The expander is removed during the subsequent saponification operation and reinserted thereafter remaining inside the cake throughout the remaining operations. The use of the fabric sock offers many advantages; thus, the handling of the cake is effected without damage to the yarn windings, the saponification and subsequent operations are to impart thereto a rela-' cifected in a more uniform manner resulting in a more uniform product, and the fabric sock surrounding the cake also acts as a filtering medium preventing the passage therethrough of any extraneous substances which may be present in the treating liquids. It is to be understood that the sock may be made of any other suitable material such as, for example, circular knit cotton fabric or a suitably treated paper.
while the saponiflcation of the yarn cake may be effected in any suitable manner, I have found that optimum results, with respect to uniformity in the resulting product and speed of saponiflcation, are obtained by placing the yarn cake covered with the fabric sock in a rotating perforated spinning bucket and subjecting the yarn cake to the action of a saponifying agent comprising a solution of a basic saponifying agent. The regenerated cellulose yarn produced may be washed free of saponifying agent while still in the spinning bucket and in cake form. The saponified yarns are then dried and wound into any desired package form. The regenerated cellulose yarns produced are found to be more uniform, to have higher dry and wet tenacities, to have fewer broken ends and to be cleaner than the regenerated cellulose yarns formed by prior processes of saponifying cellulose acetate or other organic acid esters of cellulose.
The saponifying agent may be in the form of an aqueous, alcoholic or aqueous/alcoholic solution of any suitable basic agent, and may be sprayed onto the stretched cellulose acetate or other organic acid'ester of cellulose yarns in any convenient manner. The saponifying agent may be inorganic in nature such as, for example, sodium hydroxide or potassium hydroxide. Organic saponifying agents such as, for example, methyl amine, ethylene diamlne or triethanolamine, may also be employed. It is preferred that the saponifying solution also contain from about 6 to 10% by weight of sodium acetate which assists materially in preventing degradation of the yarn undergoing saponiflcation. Preferably, I employ an aqueous solution of sodium hydroxide as the saponifying agent and in concentrations of 0.1 to 5% by weight. I have obtained highly desirable results by employing a 0.6% aqueous solution of sodium hydroxide containing 8 to 10% of sodium acetate as the saponifying medium and supplying this medium to the spinning bucket at a temperature from 140 to 180 F. and at a rate of 4 gallons per minute. While the temperature of the saponiflcation medium may range from 20 to C., I have found that optimum results are obtained when the temperature of the saponiflcation medium is as stated, namely from to 180 F.
The saponiflcation medium is introduced in the center of the cake in the spinning bucket and centrifugally distributed and dispelled throughout the cake. The spinning bucket is preferably rotated at the rate of about 730 R. P. M. The cake of yarn is subjected to the saponiflcation treatment rotating spinning bucket for about 2 hours after which it is washed while still in the spinning bucket and finally dried for 24 hours at a temperature of about to F. The cake is then placed on a wood cake holder and wound into any desired package form employing conventional textile apparatus.
In the drawing:
Fig. l is a view, partly in section, showing a centrifuge in which the saponiflcation of the yarn cake is effected,
Fig. 2 is a perspective view of the yarn cake surrounding the fabric sock as it is taken ed the arbor on which the yarn cake is wound, and
Fig. 3 is a cross-sectional view of the yarn cake completely enclosed by the fabric sock.
Like reference numerals indicate like parts throughout the several views of the drawing.
Referring to the drawing, the reference numeral t indicates a tank for holding the saponifying agent which is fed through conduit 5 to a pump 6 adapted to supply the saponifying agent at the desired rate to a centrifuge generally indicated by reference numeral 1 through a conduit 8. The lower end of conduit 8 is perforated and forms a distributing header 9 extending within the centrifuge.
The centrifuge 1 comprises a spinning pump I l to which is attached a shaft i2 extending through the bottom of the outer housing i3 of the contrifuge. The shaft i2 is adapted to be rotated at the desired speed by any suitable means. The spinning bucket is provided with openings [6 in the centrifugal wall thereof in which the saponifying agent is removed as it passes through the yarn cake i5. The bottom of outer casing i3 is provided with a suitable drain or outlet I 6 which, if desired, may be connected to a pipe I! for returning the saponifying agent to the tank 4 for recycling the same.
The yarn cake i 5 which was wound on an arbor with a fabric sock i8 has the sock completely covering the same with the ends overlapping, as shown in is in Fig. 3, before it is placed in the spinning bucket ii of the centrifuge. The yarn cake is placed in the spinning bucket in such a manner that the header 9 is substantially in the middle of the opening in said yarn cake.
If desired, an annular plate 2! is placed upon the yarn cake, remaining thereon throughout the saponiflcation process. The weight of the annular plate fl is such that it will cause contraction in the yarn cake as the saponification of said yarn cake proceeds causing the denier oi the yarn forming the cake to decrease.
In order to further illustrate my invention but without being limited thereto the following example is given:
Example A filament, 32.5 denier cellulose acetate yarn which has been given a stretch of 900% is backwound with a twist of 2%; turns per inch, from the bobbins on which the yarn was taken up with a twist of turn per inch during the stretching operation, in the form of a cake on to the 'aibor of a Whitin twister cheeser, the arbor being slightly tapered and being first covered with a fabric sock. The yarn cake is wound on the fabric sock to a weight of 1.7 pounds with a traverse wind of 1 to 1% at the start of the cake. The yarn cake and the fabric sock are then removed together from the arbor, the ends of the sock are then turned on the outer windings of the yarn cake so as to cover the yarn cake completely and an expander is inserted in the covered yarn cake to maintain the shape thereof.
The fabric sock-covered yarn cake, after the expander is removed therefrom, is placed in a winning bucket and a centrifuge and an annular plate of appreciable weight is seated thereon. Saponifying liquid comprising a 0.6% aqueous solution is forced into a spinning bucket at a speed of 730 R. P. M. at the rate of 4 gallons per minute for 2 hours, the temperature of the saponifying liquid being 140 F. The saponified yarn cake is then washed for 30 minutes with softener-heated water at 140 F. and dried for 24 hours at 150 F. The expander is again inserted in the dried yarn cake and yarn of the cake is then wound into a cone.- The regenerated cellulose yarn produced by this economical method is of better quality with respect to uniformity of saponification than the regenerated cellulose produced by saponifying stretched yarn by the bobbin method. The regenerated cellulose yarn produced in accordance with my process has a dry tenacity of 7.12, a dry elongation of 6.3, a wet tenacity of 6.20 and wet elongation of 6.5.
The cellulose acetate yarns stretched and saponified in accordance with the process of this invention to yield regenerated cellulose of improved quality may be prepared by extruding a solution of cellulose'acetate dissolved in a suitable solvent through a plurality of orifices into an evaporative medium as in the dry method of spinning or into a coagulating or precipitating liquid medium as in the wet method of spinning. The filaments so formed are associated together to form the desired m-ulti-fllament yarn which are first stretched and then saponified. In addition to cellulose acetate, organic acid esters of cellulose may be employed for preparing regenerated cellulose yarns of improved tenacity. Such other organic acid esters of cellulose may be cellulose propionate, cellulose butyrate and mixed esters of cellulose, such as cellulose acetatepropionate and cellulose acetate-butyrate. The cellulose acetate or other organic acid ester of cellulose employed may be of any degree of esterlfication, for example, where cellulose acetate is employed it may have an acetyl value of from 40 to 62.5%, calculated as acetic acid.
It is to be understood that the foregoing detailed description is given merely by way of iilustration and that many variations may be made therein without departing from the spirit of my invention.
Having described my invention, what I desire to secure by Letters Patent is:
In a process for preparing regenerated cellulose yarn of increased tenacity, the steps of winding stretched yarn having a basis of an organic acid' ester of cellulose into cake form on a fabric stock while inserting a twist in said stretched yarn, completely covering said yarn cake with said fabric sock, placing said fabric covered yarn cake in a vessel rotating at a speed of 730 R. P. M., feeding a saponifylng medium comprising a 0.6% aqueous solution of sodium hydroxide, containing 8 to 10% of sodium acetate, at a temperature of F. into the rotating vessel at a rate of 4 gallons per minute to convert said organic acid ester of cellulose yarn into regenerated cellulose yarn, and winding said regenerated cellulose yarn from cake form into another form of yarn package.
CAMILLE DREYFUS.
REFERENCES CITED The following references are of record in the file of this patent: V
UNITED STATES PATENTS Number Name Date 2,002,481 Gordon, Jr., et ai. May 21, 1935 2,053,767 Dreyfus Sept. 8, 1936 2,087,948 Chatin July 27, 1937 2,145,004 melmann Jan. 24, 1939 Certificate of Correction Patent No. 2,506,710 May 9, 1950 CAMILLE DREYFUS It is hereby certified that errors appear in the printed specification of the above numbered patent requiring correction as follows:
Column 6, line 3, for softener-heated read softener-treated; line 50, for the Word stock read sock; and that the said Letters Patent should be read With these corrections therein that the same may conform to the record of the case in the Patent Ofice.
Signed and sealed this 22nd day of August, A. D. 1950.
[SEAL] THOMAS F. MURPHY,
Assistant Oommz'ssioner of Patents.
hiM
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US720070A US2506710A (en) | 1947-01-03 | 1947-01-03 | Production of high tenacity filamentary materials |
GB183/48A GB652745A (en) | 1947-01-03 | 1948-01-02 | Improvements relating to the saponification of filamentary material of an organic ester of cellulose |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US720070A US2506710A (en) | 1947-01-03 | 1947-01-03 | Production of high tenacity filamentary materials |
Publications (1)
Publication Number | Publication Date |
---|---|
US2506710A true US2506710A (en) | 1950-05-09 |
Family
ID=24892509
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US720070A Expired - Lifetime US2506710A (en) | 1947-01-03 | 1947-01-03 | Production of high tenacity filamentary materials |
Country Status (2)
Country | Link |
---|---|
US (1) | US2506710A (en) |
GB (1) | GB652745A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1272694A1 (en) * | 2000-03-27 | 2003-01-08 | SK Chemicals Co., Ltd. | Cellulosic materials having composite crystalline structure |
JP2007107145A (en) * | 2005-10-14 | 2007-04-26 | Kawasaki Nenshi Kk | Method for spinning |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2002481A (en) * | 1931-09-10 | 1935-05-21 | Skenandoa Rayon Corp | Artificial silk manufacture |
US2053767A (en) * | 1932-02-19 | 1936-09-08 | Dreyfus Henry | Production of filaments, yarns, fabrics, and like materials |
US2087946A (en) * | 1930-10-22 | 1937-07-27 | Du Pont | Process for finishing artificial thread |
US2145004A (en) * | 1933-07-28 | 1939-01-24 | Ig Farbenindustrie Ag | Manufacture of artificial silk |
-
1947
- 1947-01-03 US US720070A patent/US2506710A/en not_active Expired - Lifetime
-
1948
- 1948-01-02 GB GB183/48A patent/GB652745A/en not_active Expired
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2087946A (en) * | 1930-10-22 | 1937-07-27 | Du Pont | Process for finishing artificial thread |
US2002481A (en) * | 1931-09-10 | 1935-05-21 | Skenandoa Rayon Corp | Artificial silk manufacture |
US2053767A (en) * | 1932-02-19 | 1936-09-08 | Dreyfus Henry | Production of filaments, yarns, fabrics, and like materials |
US2145004A (en) * | 1933-07-28 | 1939-01-24 | Ig Farbenindustrie Ag | Manufacture of artificial silk |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1272694A1 (en) * | 2000-03-27 | 2003-01-08 | SK Chemicals Co., Ltd. | Cellulosic materials having composite crystalline structure |
EP1272694A4 (en) * | 2000-03-27 | 2009-05-13 | Sk Chemicals Co Ltd | Cellulosic materials having composite crystalline structure |
JP2007107145A (en) * | 2005-10-14 | 2007-04-26 | Kawasaki Nenshi Kk | Method for spinning |
Also Published As
Publication number | Publication date |
---|---|
GB652745A (en) | 1951-05-02 |
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