US2974005A - Manufacture of rayon - Google Patents

Manufacture of rayon Download PDF

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Publication number
US2974005A
US2974005A US738950A US73895058A US2974005A US 2974005 A US2974005 A US 2974005A US 738950 A US738950 A US 738950A US 73895058 A US73895058 A US 73895058A US 2974005 A US2974005 A US 2974005A
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United States
Prior art keywords
yarn
viscose
solution
bath
spinneret
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Expired - Lifetime
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US738950A
Inventor
Heuer Kurt
Arnold L Mcpeters
Albin F Knight
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Akzona Inc
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American Enka Corp
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Filing date
Publication date
Priority to NL212326D priority Critical patent/NL212326A/xx
Priority to BE560509D priority patent/BE560509A/xx
Priority to NL109819D priority patent/NL109819C/xx
Priority to CH4914057A priority patent/CH363122A/en
Priority to DEA27662A priority patent/DE1208846B/en
Priority to GB25681/57A priority patent/GB871334A/en
Priority to FR1182556D priority patent/FR1182556A/en
Application filed by American Enka Corp filed Critical American Enka Corp
Priority to US738950A priority patent/US2974005A/en
Priority to BE578637A priority patent/BE578637R/en
Priority to CH7316359A priority patent/CH367272A/en
Priority to ES0249596A priority patent/ES249596A2/en
Priority to GB18297/59A priority patent/GB879995A/en
Priority to FR796310A priority patent/FR75813E/en
Application granted granted Critical
Publication of US2974005A publication Critical patent/US2974005A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • HELECTRICITY
    • H04ELECTRIC COMMUNICATION TECHNIQUE
    • H04QSELECTING
    • H04Q3/00Selecting arrangements
    • H04Q3/0008Selecting arrangements using relay selectors in the switching stages
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F2/00Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
    • D01F2/06Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
    • D01F2/08Composition of the spinning solution or the bath
    • D01F2/10Addition to the spinning solution or spinning bath of substances which exert their effect equally well in either
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01HELECTRIC SWITCHES; RELAYS; SELECTORS; EMERGENCY PROTECTIVE DEVICES
    • H01H67/00Electrically-operated selector switches
    • H01H67/22Switches without multi-position wipers

Definitions

  • the present invention relates to the manufacture of rayon yarn, and more particularly to the production of high tenacity viscose rayon yarn that is characterized by its excellent fatigue resistance and improved strength which makes it especially suitable for use in reinforcing rubber articles such as cord tires and the like.
  • the amount of Ethoquad added to the viscose can vary within a limited range but for the best results it has been determined that from 2% to 4% based on oven dry, recoverable cellulose in viscose should be used.
  • this term is abbreviated to CiV, i.e., cellulose in viscose.
  • CiV i.e., cellulose in viscose.
  • the temperature of the coagulating bath should be in a range of 47-57" C. for beneficial effects, and consistently the best results are obtained when the temperature of the spinbath is in a range of 48-52 C.
  • the concen ration of zinc sulphate in the spinbath is in a range of 4.5-6.0%.
  • a spinneret assembly is preferably used of the type shown in U.S. Patent No. 2,834,046, and while the length of the tube is not critical, good results have been obtained when using one from 24 to 36 inches in length depending on the spinning speed.
  • Example I A viscose was prepared from wood pulp using 7.76% cellulose and 5.9% total alkali. Th viscose was then aged to give a NH Cl number of 20. Immediately before spinning (extruding) the viscose, a water solution was injected containing enough Ethoquad C/25 to provide the viscose with 2.5% CiV. This dilution lowered the viscose composition to 7.5/5.7 and the NH Cl number was lowered to 18. This viscose was spun into a coagulating bath having a composition of 4.8%
  • Example I Viscoses were prepared and spun under the same conditions as in Example 1, except that they contained 3.0% Ethoquad C/25 CW, and the spinbath temperature was lowered to 49 C. The samples differed only in the amount of Ethomeen C/ZS" added to the spinbath. The averages of the singles (yarn) and cord properties are tabulated below:
  • a process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and 800- 2000 p.p.m. of a long chain aliphatic tertiary amineethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
  • a process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and at least 400 p.p.m. of a long chain aliphatic tertiary amine-ethylene oxide condensate to form a filamentary yarn therefrom, passing the thus formed yarn to a second hot bath and during passing therethrough stretching the yarn at least 100%.
  • a process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into a confined aqueous sulphuric acid coagulating bath containing zinc sulphate and at least 400 p.p.m. of a long chain aliphatic tertiary amine- 6o ethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
  • a process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises in corporating a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into a bath maintained at a temperature of 48-62 C. and containing sulphuric acid, sodium sulphate, zinc sulphate and at least 400 p.p.m. of a long chain aliphatic tertiary amine-ethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
  • a process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating a quaternary derivative of an ethoxylated amine into a viscose solution having a maturity in a range of l720 NH Cl number, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and at least 400 p.p.m. of a long chain aliphatic tertiary amineethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
  • a process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating about 2.5% CiV of a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and 800-2000 p.p.m. of a long chain aliphatic tertiary amine-ethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
  • a process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating into a viscose solution a modifier of the following formula:
  • R represents an alkyl radical containing at least six carbon atoms, x+y equal fifteen, and Z is an anion, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and 800 to 2000 p.p.m. of a long chain aliphatic tertiary amine-ethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.

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  • Engineering & Computer Science (AREA)
  • Computer Networks & Wireless Communication (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Textile Engineering (AREA)
  • Artificial Filaments (AREA)

Description

2,974,005 MANUFACTURE OF RAYON Kurt Heuer, Crehben, Germany, Arnold L. McP-eters, West Asheville, and Albin F. Knight, Asheville, N.C., assignors to American Enka Corporation, Erika, NC, a corporation of Delaware No Drawing. Filed June 2, 1958, Ser. No. 738,950 7 Claims. (Cl. 18--54) The present invention relates to the manufacture of rayon yarn, and more particularly to the production of high tenacity viscose rayon yarn that is characterized by its excellent fatigue resistance and improved strength which makes it especially suitable for use in reinforcing rubber articles such as cord tires and the like.
In an effort to meet the ever increasing competition in this particular field, research efforts are continuing at a high rate among all of the rayon producers with the result that higher quality yarns, particularly with respect to strength and fatigue resistance, are being developed.
One of the most significant developments has been the use of modifiers of the type disclosed in application Serial No. 609,792, filed September 14, 1956 (having common ownership herewith). These compounds are known as Ethoquads and reference is made to the aforesaid application for the chemical and structural formula, but will be spoken of generally in this application as a quaternary derivative of an ethoxylated amine.
Another class of compounds that have been successfully used as modifiers is disclosed in U.S. Patent No. 2,572,217, and reference is made to that patent for the structural and chemical formula of these compounds which are known as Ethomeens, but in this application these compounds will be generally referred to as a long chain aliphatic tertiary amine-ethylene oxide condenate.
It is therefore the object of the present invention to provide an improved process that within certain critical limits will produce an even higher strength yarn than has heretofore been manufactured.
Applicants have now determined that under certain rather critical conditions, a rayon yarn can be produced that is from to 10% higher in yarn and cord strengths than the yarns normally produced with modifiers. This improved process resulted unexpectedly from using an Ethomeen in the acid coagulating bath in very low concentrations while at the same time using the Ethoquad as a modifier in a manner similar to the aforesaid application, provided that certain specific spinning condi tions are observed and followed. It is not known precisely why the use of an Ethomeen in the spinbath in such low concentrations improves the resulting product so significantly, because at such low concentrations it is doubtful whether this chemical will have any strong modifying action on the yarn; but in any event, and for whatever reason, in actual practice the strength of the yarn has been improved while the fatigue resistance is not changed, or may be even improved, or in other words, the flexing life of the yarn is not disturbed by this increase in tensile strength.
The amount of Ethoquad added to the viscose can vary within a limited range but for the best results it has been determined that from 2% to 4% based on oven dry, recoverable cellulose in viscose should be used. Hereinafter, this term is abbreviated to CiV, i.e., cellulose in viscose. The best results are attained if the addition of the Ethoquad to the viscose solution is made in a manner similar to that disclosed in application Serial No.
678,766, filed August 19, 1957 (having common ownership herewith); namely, injecting the Ethoquad into a flowing stream of viscose, thoroughly mixing the modifier with the viscose and then immediately spinning the mixture into an acid coagulating bath to form filamentary arn therefrom.
States Patent 0 Patented Mar. 7, 1961 The effectiveness of an Ethomeen in the spinbath is obtained only within a substantially narrow range of conditions which are as follows:
One of the most essential conditions is that the viscose maturity must be high and the best results are obtained in a range from 17-20 NH Cl number. 3
Some improvement is obtained with as little as 400 p.p.m. of Ethomeen in the spinbath, but in order to obtain the maximum improvement possible, from 800 to 2000 ppm. are required, depending on other spinning conditions.
The temperature of the coagulating bath should be in a range of 47-57" C. for beneficial effects, and consistently the best results are obtained when the temperature of the spinbath is in a range of 48-52 C. The concen ration of zinc sulphate in the spinbath is in a range of 4.5-6.0%.
A spinneret assembly is preferably used of the type shown in U.S. Patent No. 2,834,046, and while the length of the tube is not critical, good results have been obtained when using one from 24 to 36 inches in length depending on the spinning speed.
Specific conditions showing improvements in the yarn and cord strengths are given in the following examples, wherein a control was run with no Ethomeen in the spinbath and compared with the use of 400, 800, and 1800 p.p.m. of Ethomeen in the spinbath.
Example I A viscose was prepared from wood pulp using 7.76% cellulose and 5.9% total alkali. Th viscose was then aged to give a NH Cl number of 20. Immediately before spinning (extruding) the viscose, a water solution was injected containing enough Ethoquad C/25 to provide the viscose with 2.5% CiV. This dilution lowered the viscose composition to 7.5/5.7 and the NH Cl number was lowered to 18. This viscose was spun into a coagulating bath having a composition of 4.8%
H 12% Na SO and 5.0% ZnSO while maintaining the temperature of the bath at approximately 51 C. The viscose was extruded through an 1100 hole spinneret to produce a yarn of 1925 total denier consisting of 1100 filaments. A tube was mounted on the spinneret which was 32 inches in length with a uniform diameter. From the coagulating bath, the yarn was passed over a godet for two 20-inch dips into a second bath having a composition of 4.0% H 80 1.3% Na SO and 0.3% 21180 while being maintained at a temperature of approximately C. During immersion in the second bath, the yarn was stretched 111%. The final speed of the yarn was 55 meters per minute and the yarn was collected in cake form in a centrifugal pot. The cake was washed acid-free, purified, and dried. Finally, it was slashed 11% in an oil emulsion and formed into cords.
A number of samples were spun under exactly the same conditions described above, except that the amount of Ethomeen C/ 25 added to the spinbath was changed. The averages of the resulting singles (yarn) and cord properties are tabulated below.
Ethomeen O/25inSpinbath,p.p.m. I 0 I 400 I 800 Unslashed Singles:
3 Example I] Viscoses were prepared and spun under the same conditions as in Example 1, except that they contained 3.0% Ethoquad C/25 CW, and the spinbath temperature was lowered to 49 C. The samples differed only in the amount of Ethomeen C/ZS" added to the spinbath. The averages of the singles (yarn) and cord properties are tabulated below:
Ethomeen /25 in Spinbath, p.p.m. 0 S00 1800 Unslashed Singles:
Conditioned Strength, g./l00 d 463 464 492 Conditioned Elongation, percent 22,8 22.0 21.8 Slashed Singles:
Ethorneen 0/25 Ethoquad 0/25 It-N derived from coconut fatty acids. :c-l- 15.
it is to be understood that the invention is intended to be limited only to the scope of the appended claims.
What is claimed is:
1. A process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and 800- 2000 p.p.m. of a long chain aliphatic tertiary amineethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
2. A process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and at least 400 p.p.m. of a long chain aliphatic tertiary amine-ethylene oxide condensate to form a filamentary yarn therefrom, passing the thus formed yarn to a second hot bath and during passing therethrough stretching the yarn at least 100%.
3. A process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into a confined aqueous sulphuric acid coagulating bath containing zinc sulphate and at least 400 p.p.m. of a long chain aliphatic tertiary amine- 6o ethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
4. A process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises in corporating a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into a bath maintained at a temperature of 48-62 C. and containing sulphuric acid, sodium sulphate, zinc sulphate and at least 400 p.p.m. of a long chain aliphatic tertiary amine-ethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
'5. A process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating a quaternary derivative of an ethoxylated amine into a viscose solution having a maturity in a range of l720 NH Cl number, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and at least 400 p.p.m. of a long chain aliphatic tertiary amineethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
6. A process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating about 2.5% CiV of a quaternary derivative of an ethoxylated amine into a viscose solution, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and 800-2000 p.p.m. of a long chain aliphatic tertiary amine-ethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
7. A process for the production of high tenacity, highly fatigue resistant, viscose rayon yarn which comprises incorporating into a viscose solution a modifier of the following formula:
;CH2CH20);H R--N z- CHz-CH2OMH OH: in which R represents an alkyl radical containing at least six carbon atoms, x+y equal fifteen, and Z is an anion, extruding the solution through a spinneret into an aqueous sulphuric acid coagulating bath containing zinc sulphate and 800 to 2000 p.p.m. of a long chain aliphatic tertiary amine-ethylene oxide condensate to form a filamentary yarn therefrom and withdrawing the yarn from the bath and aftertreating the same.
References Cited in the file of this patent UNITED STATES PATENTS 2,696,423 Dietrich Dec. 7, 1954 2,784,107 Tallis et al. Mar. 5, 1957 2,852,334 Hollihan et a1 Sept. 16, 1958 FOREIGN PATENTS 741,727 Great Britain Dec. 4, 1955

Claims (1)

1. A PROCESS FOR THE PRODUCTION OF HIGH TENACITY, HIGHLY FATIGUE RESISTANT, VISCOSE RAYON YARN WHICH COMPRISES INCORPORATING A QUATERNARY DERIVATIVE OF AN ETHOXYLATED AMINE INTO A VISCOSE SOLUTION, EXTRUDING THE SOLUTION THROUGH A SPINNERET INTO AN AQUEOUS SULPHURIC ACID COAGULATING BATH CONTAINING ZINC SULPHATE AND 8002000 P.P.M. OF A LONG CHAIN ALIPHATIC TERTIARY AMINEETHYLENE OXIDE CONDENSATE TO FORM A FILAMENTARY YARN THEREFROM AND WITHDRAWING THE YARN FROM THE BATH AND AFTERTREATING THE SAME.
US738950A 1956-09-14 1958-06-02 Manufacture of rayon Expired - Lifetime US2974005A (en)

Priority Applications (13)

Application Number Priority Date Filing Date Title
NL212326D NL212326A (en) 1956-09-14
BE560509D BE560509A (en) 1956-09-14
NL109819D NL109819C (en) 1956-09-14
DEA27662A DE1208846B (en) 1956-09-14 1957-08-05 Process for the production of artificial structures such as threads, tapes and films from cellulose hydrate
CH4914057A CH363122A (en) 1956-09-14 1957-08-05 Process for the production of artificial threads, ribbons, films and the like from viscose and structures produced by this process
GB25681/57A GB871334A (en) 1956-09-14 1957-08-14 A process for the production of artificial threads, bands, films and like products from viscose
FR1182556D FR1182556A (en) 1956-09-14 1957-09-10 Process for the production of artificial yarns, webs, films and the like from viscose and products so obtained
US738950A US2974005A (en) 1956-09-14 1958-06-02 Manufacture of rayon
BE578637A BE578637R (en) 1958-06-02 1959-05-12 Process for the manufacture of artificial threads, tapes, films and the like from viscose, as well as the products thus manufactured
CH7316359A CH367272A (en) 1956-09-14 1959-05-13 Process for the production of artificial threads, ribbons, films etc. from viscose, as well as structures produced by this process
ES0249596A ES249596A2 (en) 1958-06-02 1959-05-23 A procedure for the production of threads, bands, films and similar artificial products from viscosa (Machine-translation by Google Translate, not legally binding)
GB18297/59A GB879995A (en) 1956-09-14 1959-05-29 A process for the production of artificial threads, bands, films and like products from viscose
FR796310A FR75813E (en) 1956-09-14 1959-06-02 Process for the production of artificial yarns, webs, films and the like from viscose, and products so obtained

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US60979256A 1956-09-14 1956-09-14
US738950A US2974005A (en) 1956-09-14 1958-06-02 Manufacture of rayon

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US2974005A true US2974005A (en) 1961-03-07

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US738950A Expired - Lifetime US2974005A (en) 1956-09-14 1958-06-02 Manufacture of rayon

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US (1) US2974005A (en)
BE (1) BE560509A (en)
CH (2) CH363122A (en)
DE (1) DE1208846B (en)
FR (1) FR1182556A (en)
GB (2) GB871334A (en)
NL (2) NL109819C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012120074A1 (en) * 2011-03-08 2012-09-13 Sappi Netherlands Services B.V. Method for spinning anionically modified cellulose and fibres made using the method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2696423A (en) * 1951-05-29 1954-12-07 Du Pont Viscose modifiers
US2784107A (en) * 1951-12-13 1957-03-05 Courtaulds Ltd Production of artificial filaments, threads and the like
US2852334A (en) * 1954-11-03 1958-09-16 American Viscose Corp Method of producing viscose rayon

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2696423A (en) * 1951-05-29 1954-12-07 Du Pont Viscose modifiers
GB741727A (en) * 1951-05-29 1955-12-14 Du Pont Manufacture of regenerated cellulose structures from viscose
US2784107A (en) * 1951-12-13 1957-03-05 Courtaulds Ltd Production of artificial filaments, threads and the like
US2852334A (en) * 1954-11-03 1958-09-16 American Viscose Corp Method of producing viscose rayon

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012120074A1 (en) * 2011-03-08 2012-09-13 Sappi Netherlands Services B.V. Method for spinning anionically modified cellulose and fibres made using the method
US9187848B2 (en) 2011-03-08 2015-11-17 Sappi Netherlands Services B.V. Method for spinning anionically modified cellulose and fibres made using the method
EA024783B1 (en) * 2011-03-08 2016-10-31 Саппи Нидерландс Сервисез Б.В. Method for spinning anionically modified cellulose
KR101916978B1 (en) 2011-03-08 2018-11-08 사피 네덜란드 서비시즈 비.브이. Method for spinning anionically modified cellulose and fibres made using the method

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Publication number Publication date
DE1208846B (en) 1966-01-13
CH367272A (en) 1963-02-15
NL212326A (en)
FR1182556A (en) 1959-06-26
NL109819C (en)
GB879995A (en) 1961-10-11
GB871334A (en) 1961-06-28
BE560509A (en)
CH363122A (en) 1962-07-15

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