US2359750A - Viscose spinning solution - Google Patents

Viscose spinning solution Download PDF

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US2359750A
US2359750A US396543A US39654341A US2359750A US 2359750 A US2359750 A US 2359750A US 396543 A US396543 A US 396543A US 39654341 A US39654341 A US 39654341A US 2359750 A US2359750 A US 2359750A
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polyoxyethylene
spinning
glycol ethers
per molecule
esters
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US396543A
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Benjamin W Collins
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Akzo Nobel UK PLC
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American Viscose Corp
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Priority claimed from US389325A external-priority patent/US2359749A/en
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Priority to US751136A priority patent/US2519227A/en
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    • 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
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S516/00—Colloid systems and wetting agents; subcombinations thereof; processes of
    • Y10S516/01—Wetting, emulsifying, dispersing, or stabilizing agents

Definitions

  • This invention has for its principal object to provide improvements in the spinning operation employed in the manufacture of synthetic shapes such as yarns, filaments, films and the like.
  • the compounds contemplated by the invention are the polyethylene glycol ethers of organic compounds having at least one functional aliphatic hydroxyl group and containing at least one hydrophobic group comprising a hydrocarbon chain of at least 8 carbon atoms, such as alcohols and polyhydric alcohols, hydroxy carboxylic acids, hydroxy esters, epoxy alcohols and hydroxy epoxy esters; polyethylene glycol esters of compounds having at least one functional aliphatic carboxyl group and containing at least one hydrophobic group comprising a hydrocarbon chain of at least 8 carbon atoms, such as fatty acids, polycarboxylic acids, hydroxy fatty acids, and epoxy fatty acids; polyethylene glycol acetals of organic compounds having at least one functional aliphatic aldehyde group and containing at least one hydrophobic group comprising a hydrocarbon chain of at least 8 carbon atoms, such as aliphatic aldehydes, aldoses; and polyethylene glycol ether-esters, ether-acetals, ester
  • the compounds are nonionogenic, rela- 1 tively chemically unreactive, substantially stable under spinning conditions, and contain no free functional groups other than aliphatic hydroxy] or carbonyl.
  • the compounds may contain ether, ester, acetal, or hemiacetal groups which are substantially stable under the conditions of spinning.
  • the stability herein referred to is such stability that the compounds, prior to their complete decomposition in the spinning solution or the spinning bath, will exert their favorable influence in preventing clogging of the openings in the spinnerets and in thereby maintaining uniformity of filament size.
  • Caprylic acid esters of polyoxyethylene glycols Pelargonic acid esters of polyoxyethylene glycols Capric acid esters of polyoxyethylene glycols Erasmus acid esters of polyoxyethylene glycols Myristic acid esters of polyoxyethylene glycols Palmitic acid esters of polyoxyethylene glycols Margaric acid esters of polyoxyethylene glycols Stearic acid esters of polyoxyethylene glycols Oleic acid esters of polyoxyethylene glycols Ricinoleic acid esters of polyoxyethylene glycols Hydroxy stearic acid esters of polyoxyethylene glycols Octyl' ethers of polyoxyethylene glycols Decyl ethers of polyoxyethylene glycols Dodecyl ethers of polyoxyethylene glycols Tetradecyl ethers of polyoxyethylene glycols Hexadecyl ethers of polyoxyethylene glycols Octadecylethers of polyoxyethylene glycols Cetyl ethers of polyoxyethylene glycols Montanyl ethers of poly
  • Polyoxyethylene glycol ethers of mannita monolaurate Polyoxyethylene glycol ethers of sorbitan monolaurate Polyoxyethylene glycol ethers of sorbitan monooleate acyl glycol ethers of mannitan monomyristate Polyoxyethylene glycol ethers of mannitan mono.
  • polyethylene glycol group or groups may be connected in the same compound by either or both ether and ester groups depending upon the parent substances from which they are derived and the method of producing the compounds therefrom.
  • oxyethylene units may replace the hydrogen
  • all Of the oxyethylene units may be in a single chain or theymay be present in the compound in the form 01 two or more chains, the latter situation being common when the compound is produced by reacting ethylene oxide with a parent substance having at least two functional groups whether hydroxyl, aldehyde, carboxyl or any combination of these three. It is only essential that the total number of oxyethylene units in the one or more chains add up to a total of at least eight. Some or all of the oxyethylene units or chains of such units may have either or both of their'ends connected to the remainder of, the compound through ether, ester or acetal linkages. I
  • the common methods of making the compounds with which the invention is concerned generally result in the formation of mixtures of compounds having a greater or less number of oxyethylene units per molecule and analytical determinations of such complex mixtures indicate the average number of such units per molecule throughout the mass of the compound analyzed.
  • the compounds employed in accordance with this invention may comprise molecules containing less than 8 oxyethylene units in admixture with'others containing 8 or more'such units. Accordingly, in the specification' and the claims the definition of these compounds is intended to include not only those having a uniform and constant constitution throughout but also such complexmixtures as have an effective portion containing at' least 8 oxyethylene units per molecule.
  • the various surface active compounds may be produced in any suitable manner. Generally, they may be produced by reacting ethylene oxide with the selected fatty acid, alcohol, hydroxy fatty acid, hydroxy fatty acid ester or related compound within the scope of the general class described above.
  • the reaction products of ethylene oxide with sorbitan monolaurate may be prepared by introducing sorbitan monolaurate with a small amount of sodium methylate as a catalyst into a stirring autoclave and raising the temperature to C., gradually adding ethylene oxide to this mixture and maintaining the temperature between C. and
  • the degree to which the reaction with the ethylene oxide is carried out depends upon the compound with which it is reacted and the character of the spinning solution or precipitating bath in which it is to be used. The reaction is carried out to such a degree that the reaction products are soluble in the spinning bath or spinning solution in which they are used.v
  • the invention is applicable in forming regenerated cellulose shapes by extruding viscose solution into an acid precipitating bath and is found particularly advantageous where the precipitating bath contains a high concentration of metallic salts, especially zinc, in concentrations of the order of 3% to 10%.
  • the invention is also advantageous in spinning other cellulose solutions including cuprammonium and cellulose derivatives such as cellulose acetate as well as other synthetic materials, including cop'olymers of vinyl chloride and vinyl acetate.
  • a small amount of the surface active material of the same order may be dissolved in the precipitating medium or may be added to both the spinning solution and the precipitating medium.
  • a multifllament regenerated cellulos am is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of and between 0.02 and 0.03% of organic compounds comprising a sorbitan monolaurate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyethylene units per molecule.
  • a multifllament regenerated cellulose yarn is formed-by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a sorbitan monolaurate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 8 oxyethylene units per molecule.
  • a multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid' spinning bath containing a high concentatlon of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a sorbitan monooleate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyethylene units per molecule.
  • a multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentation of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a mannitan monomyristate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyethylene units per molecule.
  • a multifllament regenerated cellulose yarn is formed by, extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a mannitan monolaurate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oiwethylene units per molecule.
  • a multifllament regenerated cellulose yarn is formed by extruding a viscose solution through a spinneret into an aqueous sulphuric acid spinning bathcontaining a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a mannitan monooleate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyetln'lene units per molecule.
  • a multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02
  • mannitan monopalmitate having atleast 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyethylene units per molecule.
  • a multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between v a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising lauryl alcohol in which the hydroxyl group has been replaced by a 'hydroxy polyoxyethylene group and the average oxyethylene content is 20 oxyethylene units per molecule.
  • a multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising triricinolein in which at least 1 free hydroxyl group has been replaced 'by a hydroxy polyoxyethylene group and the average oxyethylene content is 20 oxyethylene units per molecule.
  • a viscosespinning solution containing a small amount of a substantially stable surface achydrophobic group containing at least 8 carbon atoms in a straight chain and at least one polyoxyethylene group, the oxyethylene content being at least 8 oxyethylene units per molecule and a suiiicient number of such units in excess of eight to render the hexitan derivative substantially soluble in the viscose solution.
  • a viscose spinning solution containing a small amount of a substituted sorbitan monolaurate having at least one polyoxyethylene and 0.03% of organic compounds comprising .a 25
  • the oxyethylene content being at least 8 oxyethylene units per molecule and a sumcient content being at least 8 oxyethylene units per molecule and a, sufficient number of such units in excess of 8 to render the alcohol condensation product substantially soluble in a viscose solution.

Description

Patented Oct. 10, 1%44 VISCOSE SPINNING SOLUTION Benjamin WQCollins, Swarthmore, Pa., assignor to American Viscose Corporation, Wilmington, Del., a corporation of Delaware No Drawing. Original application April 19, 1941,
Serial No. 389,325. Divided and this application June 4, 1941, Serial No. 396,543
7 Claims.
spun by extruding the solution through a spinneret or jet having a minute opening or openings into a coagulating or precipitating medium. During the spinning operation obstructions tend to form in the minute openings in the spinneret or jet and they become fouled or clogged. This results, in the case of yarn or filament spinning, in a lack of uniformity in the filament sizes and weak and broken filaments in the finished product and,.in the case of producing films, in a lack of uniformity in thickness. In order to avoid these dimculties it is the present practice to inspect the spinnerets or jets at short intervals of time and replace those in which the openings have become fouled. This interrupts the continuity of the spinning operation and causes delays which are time consuming and costly.
This invention has for its principal object to provide improvements in the spinning operation employed in the manufacture of synthetic shapes such as yarns, filaments, films and the like.
Other objects of the invention will be apparentfrom the following description and appended claims.
It has now been found that fouling of the spinnerets and the need for frequent inspection and replacement and the lack of uniformity in yarns, filaments and films can be largely eliminated by extruding the spinning solution in the presence of a small amount of a surface active, non-ionogenic organic compound comprising at least one hydrophobic group having a hydrocarbon chain of at least 8 carbon atoms and a hydrophilic polyoxyethylene content sumcient to render the compound water-soluble so that it is readily soluble in the spinning bath or in the spinning solution. The polyoxyethylene content should be at least 8 oxyethylene units per molecule. Generally, the greater the extent to which the compound is hydrophobic, the larger th number of oxyethylene units that are required to render the compound sufliciently soluble for the purposes of the invention. I
In general, the compounds contemplated by the invention are the polyethylene glycol ethers of organic compounds having at least one functional aliphatic hydroxyl group and containing at least one hydrophobic group comprising a hydrocarbon chain of at least 8 carbon atoms, such as alcohols and polyhydric alcohols, hydroxy carboxylic acids, hydroxy esters, epoxy alcohols and hydroxy epoxy esters; polyethylene glycol esters of compounds having at least one functional aliphatic carboxyl group and containing at least one hydrophobic group comprising a hydrocarbon chain of at least 8 carbon atoms, such as fatty acids, polycarboxylic acids, hydroxy fatty acids, and epoxy fatty acids; polyethylene glycol acetals of organic compounds having at least one functional aliphatic aldehyde group and containing at least one hydrophobic group comprising a hydrocarbon chain of at least 8 carbon atoms, such as aliphatic aldehydes, aldoses; and polyethylene glycol ether-esters, ether-acetals, ester-acetals or ether-ester-acetals of organic compounds having various combinations of hydroxyl, aldehyde and carboxyl groups and containing at least one hydrophobic group comprising a hydrocarbon chain of at least 8 carbon atoms, such as hydroxy fatty acids, polyhydroxy fatty acids, aldoses, and -uronic acids. The compounds are nonionogenic, rela- 1 tively chemically unreactive, substantially stable under spinning conditions, and contain no free functional groups other than aliphatic hydroxy] or carbonyl. The compounds may contain ether, ester, acetal, or hemiacetal groups which are substantially stable under the conditions of spinning. The stability herein referred to is such stability that the compounds, prior to their complete decomposition in the spinning solution or the spinning bath, will exert their favorable influence in preventing clogging of the openings in the spinnerets and in thereby maintaining uniformity of filament size.
The following are examples of specific compounds that may be used in carrying out this invention:
Caprylic acid esters of polyoxyethylene glycols Pelargonic acid esters of polyoxyethylene glycols Capric acid esters of polyoxyethylene glycols Laurie acid esters of polyoxyethylene glycols Myristic acid esters of polyoxyethylene glycols Palmitic acid esters of polyoxyethylene glycols Margaric acid esters of polyoxyethylene glycols Stearic acid esters of polyoxyethylene glycols Oleic acid esters of polyoxyethylene glycols Ricinoleic acid esters of polyoxyethylene glycols Hydroxy stearic acid esters of polyoxyethylene glycols Octyl' ethers of polyoxyethylene glycols Decyl ethers of polyoxyethylene glycols Dodecyl ethers of polyoxyethylene glycols Tetradecyl ethers of polyoxyethylene glycols Hexadecyl ethers of polyoxyethylene glycols Octadecylethers of polyoxyethylene glycols Cetyl ethers of polyoxyethylene glycols Montanyl ethers of polyoxyethylene glycols Oleyl ethers of polyoxyethylene glycols Polyoxyethylene Polyoxyethylene glycol ethersof-diethylene glycol monoacyl esters Polyoxyethylene glycol ethers of polyethylene glycol monoacyl esters Polyoxyethylene glycol ethers of propylene glycol monoacyl esters Polyoxyethylene glycol ethers of glycerol monoacyl esters Polyoxyethylene glycol ethers of glycerol diaoyl esters Polyoxyethylene glycol ethers of polyglycerol acyl partial esters Polyoxyethylene glycol ethers of erythritol acyl partial esters Polyox-yethylene glycol ethers of pentaerythritol acyl partial esters Polyoxyethylene glycol ethers of hexitol acyl partial esters Polyoxyethylene glycol ethers of mannitol acyl partial esters Polyoxyethylene glycol ethers of sorbitol acyl partial esters Polyoxyethylene glycol ethers of hexitan acyl partial esters Polyoxyethylene glycol ethers of mannitan acyl partial esters Polyoxyethylene glycol ethers of sorbitan acyl partial esters Polyoxyethylene glycol ethers 01' hexide partial esters Polyoxyethylene' glycol ethers of mannide acyl partial esters Polyoxyethylene glycol ethers of .sorbide acyl partial esters Polyoxyethylene glycol ethers of cyclotol acyl partial esters v Polyoxyethylene glycol ethers of inositol a'cyl partialesters Polyoxyethylene glycol ethers of monosaccharide acyl partial esters Polyoxyethylene glycol ethers of oligosaccharide acyl partial esters The acyl esters may be the esters of fatty acids having 8 carbon atoms in a straight chain, such as caprylic, pelargonic, capric, lauric, myristlc, palmitic, margarlc, stearic, oleic, ricinoleic, and hydroxy stearic.
More specific combinations are:
Polyoxyethylene glycol ethers of mannita monolaurate Polyoxyethylene glycol ethers of sorbitan monolaurate Polyoxyethylene glycol ethers of sorbitan monooleate acyl glycol ethers of mannitan monomyristate Polyoxyethylene glycol ethers of mannitan mono.-
palmitate Polyoxyethylene glycol ethers of mannitan monostearate Polyoxyethylene glycol ethers of maImitan monooleate Polyoxyethyleneglycol ethers of triricinolein Polyoxyethylene glycol acetals of lauric aldehyde The polyethylene glycol group or groups may be connected in the same compound by either or both ether and ester groups depending upon the parent substances from which they are derived and the method of producing the compounds therefrom. For example, if ricinoleic acid, hydroxy stearic acid or other bi-functional compounds are reacted with ethylene oxide, part of the oxyethylene units may replace the hydrogen It should be noted that all Of the oxyethylene units may be in a single chain or theymay be present in the compound in the form 01 two or more chains, the latter situation being common when the compound is produced by reacting ethylene oxide with a parent substance having at least two functional groups whether hydroxyl, aldehyde, carboxyl or any combination of these three. It is only essential that the total number of oxyethylene units in the one or more chains add up to a total of at least eight. Some or all of the oxyethylene units or chains of such units may have either or both of their'ends connected to the remainder of, the compound through ether, ester or acetal linkages. I
The common methods of making the compounds with which the invention is concerned generally result in the formation of mixtures of compounds having a greater or less number of oxyethylene units per molecule and analytical determinations of such complex mixtures indicate the average number of such units per molecule throughout the mass of the compound analyzed. For this reason the compounds employed in accordance with this invention may comprise molecules containing less than 8 oxyethylene units in admixture with'others containing 8 or more'such units. Accordingly, in the specification' and the claims the definition of these compounds is intended to include not only those having a uniform and constant constitution throughout but also such complexmixtures as have an effective portion containing at' least 8 oxyethylene units per molecule.
The various surface active compounds may be produced in any suitable manner. Generally, they may be produced by reacting ethylene oxide with the selected fatty acid, alcohol, hydroxy fatty acid, hydroxy fatty acid ester or related compound within the scope of the general class described above. For example, the reaction products of ethylene oxide with sorbitan monolaurate may be prepared by introducing sorbitan monolaurate with a small amount of sodium methylate as a catalyst into a stirring autoclave and raising the temperature to C., gradually adding ethylene oxide to this mixture and maintaining the temperature between C. and
C. For reasons stated above, the degree to which the reaction with the ethylene oxide is carried out depends upon the compound with which it is reacted and the character of the spinning solution or precipitating bath in which it is to be used. The reaction is carried out to such a degree that the reaction products are soluble in the spinning bath or spinning solution in which they are used.v
The invention is applicable in forming regenerated cellulose shapes by extruding viscose solution into an acid precipitating bath and is found particularly advantageous where the precipitating bath contains a high concentration of metallic salts, especially zinc, in concentrations of the order of 3% to 10%. The invention is also advantageous in spinning other cellulose solutions including cuprammonium and cellulose derivatives such as cellulose acetate as well as other synthetic materials, including cop'olymers of vinyl chloride and vinyl acetate.
In carrying out the invention a small amount of the surface active material of the order of 0.01
to 0.05% may be dissolved in the spinning solution and the spinning solution is extruded into a precipitating medium. Where a liquid precipitating medium or bath is used, a small amount of the surface active material of the same order may be dissolved in the precipitating medium or may be added to both the spinning solution and the precipitating medium.
The following examples are illustrative of the invention:
1. A multifllament regenerated cellulos am is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of and between 0.02 and 0.03% of organic compounds comprising a sorbitan monolaurate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyethylene units per molecule.
2. A multifllament regenerated cellulose yarn is formed-by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a sorbitan monolaurate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 8 oxyethylene units per molecule.
3. A multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid' spinning bath containing a high concentatlon of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a sorbitan monooleate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyethylene units per molecule.
4. A multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentation of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a mannitan monomyristate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyethylene units per molecule.
5. A multifllament regenerated cellulose yarn is formed by, extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a mannitan monolaurate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oiwethylene units per molecule.
6. A multifllament regenerated cellulose yarn is formed by extruding a viscose solution through a spinneret into an aqueous sulphuric acid spinning bathcontaining a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising a mannitan monooleate having at least 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyetln'lene units per molecule.
7. A multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02
mannitan monopalmitate having atleast 1 hydroxy polyoxyethylene group per molecule and an average oxyethylene content of 20 oxyethylene units per molecule. v
8. A multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between v a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising lauryl alcohol in which the hydroxyl group has been replaced by a 'hydroxy polyoxyethylene group and the average oxyethylene content is 20 oxyethylene units per molecule.
10. A multifllament regenerated cellulose yarn is formed by extruding viscose solution through a spinneret into an aqueous sulphuric acid spinning bath containing a high concentration of zinc sulphate of the order of 5% and between 0.02 and 0.03% of organic compounds comprising triricinolein in which at least 1 free hydroxyl group has been replaced 'by a hydroxy polyoxyethylene group and the average oxyethylene content is 20 oxyethylene units per molecule.
It was found that in carrying out the spinning operation in accordance with the present invention it is necessary to change less than 50% as many spinnerets as where ordinary methods of spinning are followed. Where multifllament yarn 40 is formed the filaments are of uniform crosssection and the yarn is of generally improved quality.
While preferred embodiments of the invention have been shown, it is to be understood that changes and variations may be made without departing from the'spirit and scope of the invention as defined by the appended claims.
What I claim is:
1. A viscosespinning solution containing a small amount of a substantially stable surface achydrophobic group containing at least 8 carbon atoms in a straight chain and at least one polyoxyethylene group, the oxyethylene content being at least 8 oxyethylene units per molecule and a suiiicient number of such units in excess of eight to render the hexitan derivative substantially soluble in the viscose solution.
3. A viscose spinning solution containing a small amount of a substituted sorbitan monolaurate having at least one polyoxyethylene and 0.03% of organic compounds comprising .a 25
group, the oxyethylene content being at least 8 oxyethylene units per molecule and a sumcient content being at least 8 oxyethylene units per molecule and a, sufficient number of such units in excess of 8 to render the alcohol condensation product substantially soluble in a viscose solution.
6. A viscose spinning solution containing a small amount of a condensation product of ethylene oxide with lauryl alcohol having at least 8 oxyethylene units per molecule. 3
7. A viscose spinning solution containing a small amount of a condensation product of ethylene oxide with lauryl alcohol, having an average of about 20 oxyethylene units pen'nolecule.
BENJAIVHN W. COLLINS.
US396543A 1941-04-19 1941-06-04 Viscose spinning solution Expired - Lifetime US2359750A (en)

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Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2451558A (en) * 1944-11-06 1948-10-19 Rayonier Inc Chemically treated wood pulp and a method of producing a cellulosic product
US2459298A (en) * 1944-11-17 1949-01-18 Stamberger Paul Plastic compositions made with vulcanized, polyethylene glycol esters as plasticizers
US2481693A (en) * 1944-04-29 1949-09-13 Rayonier Inc Raw cotton for conversion into rayon
US2508036A (en) * 1950-05-16 Compounds having high wetting
US2519227A (en) * 1941-04-19 1950-08-15 American Viscose Corp Manufacture of yarns and the like
US2525786A (en) * 1948-06-18 1950-10-17 Edward M Filachione Polyhydric alcohol esters of acyloxycarboxylic acids
US2573701A (en) * 1948-06-18 1951-11-06 Edward M Filachione Polyethylene glycol esters of acyloxycarboxylic acids
US2578684A (en) * 1948-06-18 1951-12-18 Edward M Filachione Glycol esters of acyloxycarboxylic acids
US2592234A (en) * 1949-02-16 1952-04-08 Eastman Kodak Co Plasticized cellulose acetate-butyrate and cellulose acetatepropionate
US2599803A (en) * 1948-11-01 1952-06-10 Shell Dev Lubricating composition
US2665443A (en) * 1949-06-04 1954-01-12 Chicopee Mfg Corp Astatic brush for grooming the hair
US2694021A (en) * 1951-03-30 1954-11-09 Atlas Powder Co Textile bearing a starch size
US2805169A (en) * 1955-07-18 1957-09-03 Rayonier Inc High-alpha cellulose
US2892729A (en) * 1954-11-03 1959-06-30 American Viscose Corp Process of producing viscose rayon
US2895787A (en) * 1954-12-30 1959-07-21 American Viscose Corp Process of producing all skin rayon
US3240819A (en) * 1960-02-17 1966-03-15 Monsanto Co Ethenoxy-substituted alkanols
US3418405A (en) * 1962-09-10 1968-12-24 Kurashiki Rayon Co Method of manufacturing flat viscose fibers
US3431127A (en) * 1963-09-12 1969-03-04 Union Carbide Corp Process of improving the anti-blocking characteristics of regenerated cellulose tubing and the product resulting from said process

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2508036A (en) * 1950-05-16 Compounds having high wetting
US2519227A (en) * 1941-04-19 1950-08-15 American Viscose Corp Manufacture of yarns and the like
US2481693A (en) * 1944-04-29 1949-09-13 Rayonier Inc Raw cotton for conversion into rayon
US2451558A (en) * 1944-11-06 1948-10-19 Rayonier Inc Chemically treated wood pulp and a method of producing a cellulosic product
US2459298A (en) * 1944-11-17 1949-01-18 Stamberger Paul Plastic compositions made with vulcanized, polyethylene glycol esters as plasticizers
US2525786A (en) * 1948-06-18 1950-10-17 Edward M Filachione Polyhydric alcohol esters of acyloxycarboxylic acids
US2573701A (en) * 1948-06-18 1951-11-06 Edward M Filachione Polyethylene glycol esters of acyloxycarboxylic acids
US2578684A (en) * 1948-06-18 1951-12-18 Edward M Filachione Glycol esters of acyloxycarboxylic acids
US2599803A (en) * 1948-11-01 1952-06-10 Shell Dev Lubricating composition
US2592234A (en) * 1949-02-16 1952-04-08 Eastman Kodak Co Plasticized cellulose acetate-butyrate and cellulose acetatepropionate
US2665443A (en) * 1949-06-04 1954-01-12 Chicopee Mfg Corp Astatic brush for grooming the hair
US2694021A (en) * 1951-03-30 1954-11-09 Atlas Powder Co Textile bearing a starch size
US2892729A (en) * 1954-11-03 1959-06-30 American Viscose Corp Process of producing viscose rayon
US2895787A (en) * 1954-12-30 1959-07-21 American Viscose Corp Process of producing all skin rayon
US2805169A (en) * 1955-07-18 1957-09-03 Rayonier Inc High-alpha cellulose
US3240819A (en) * 1960-02-17 1966-03-15 Monsanto Co Ethenoxy-substituted alkanols
US3418405A (en) * 1962-09-10 1968-12-24 Kurashiki Rayon Co Method of manufacturing flat viscose fibers
US3431127A (en) * 1963-09-12 1969-03-04 Union Carbide Corp Process of improving the anti-blocking characteristics of regenerated cellulose tubing and the product resulting from said process

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