US3340340A - Manufacture of crimped viscose rayon fibres - Google Patents

Manufacture of crimped viscose rayon fibres Download PDF

Info

Publication number
US3340340A
US3340340A US327818A US32781863A US3340340A US 3340340 A US3340340 A US 3340340A US 327818 A US327818 A US 327818A US 32781863 A US32781863 A US 32781863A US 3340340 A US3340340 A US 3340340A
Authority
US
United States
Prior art keywords
percent
fibres
viscose
caustic soda
filaments
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US327818A
Inventor
Mytum Ernest
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Akzo Nobel UK PLC
Original Assignee
Courtaulds PLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Courtaulds PLC filed Critical Courtaulds PLC
Application granted granted Critical
Publication of US3340340A publication Critical patent/US3340340A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • 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
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/22—Formation of filaments, threads, or the like with a crimped or curled structure; with a special structure to simulate wool
    • 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
    • D01F11/00—Chemical after-treatment of artificial filaments or the like during manufacture
    • D01F11/02—Chemical after-treatment of artificial filaments or the like during manufacture of cellulose, cellulose derivatives, or proteins

Definitions

  • United States patent specification No. 2,986,446 describes a process for the manufacture of crimped viscose rayon fibres by extruding a viscose containing polyethylene glycol into an acid coagulating and regenerating bath containing zinc sulphate, stretching the filaments so formed and relaxing the stretched filaments in an aqueous medium.
  • the important properties of crimp and extensibility of the filament can be controlled by a change in one or more of the inherent features of the process, but, in general, a change which causes an increase in one property has the effect of decreasing the other.
  • the degree of crimp increases and the extensibility decreases when the filament is stretched more, whilst an increase in the zinc sulphate concentration in the bath increases the extensibility of the filament but decreases the degree of crimp.
  • the properties of the filament can, therefore, be varied between high degree of crimp and low extension on the one hand and high extension and low degree of crimp on the other.
  • the process is, however, incapable of producing a filament which combines the features of high degree of crimp and high extension.
  • Crimped staple fibres may be used as the pile of carpets.
  • the fibres should be extensible, as this contributes to their resistance to abrasion, and resilient, to preserve the appearance of the carpet during wear.
  • Viscose rayon fibres can be made more resilient by cross-linking the constituent cellulose, but this modification causes a decrease in extensibility.
  • a viscose rayon fibre suitable for cross-linking and use in carpet piles, should, therefore, be highly extensible so as to be able to tolerate the inevitable fall in extensibility which accompanies crosslinking and still retain sufiicient extensibility to maintain the resistance to abrasion.
  • a process for the production of crimped viscose rayon fibres comprises extruding a viscose containing from 5 percent to percent of cellulose, from 5 percent to 10 percent of caustic soda, more than 0.05 percent of a modifier and a zinc compound in the proportion of from 0.01 percent to 0.8 percent of zinc based on the weight of the viscose, at a salt figure of between 3 and 14, into a coagulating and regenerating bath containing from 5 percent to 14 percent of sulphuric acid, from 0.5 percent to 4 percent of zinc sulphate and more than 12 percent of sodium sulphate, to form incompletely regenerated filaments, stretching the filaments by at least 50 percent, cutting the stretched filaments into staple fibres and crimping the fibres by relaxing the fibres in a solution containing between 1 percent and 5 percent of caustic soda, before completing the regeneration of the cellulose in the fibres.
  • the increase in the extensibility of the fibre is due, in the main, to two additions to the acknowledged, known process.
  • the first of these is the use of a zinc compound, preferably an alkali metal zincate, in the viscose.
  • a zinc compound preferably an alkali metal zincate
  • This allows a desired degree of crimp to be obtained from a lower stretch, thus preserving to a greater extent the extensibility of the fibre.
  • the effect is noticeable even 3,340,340 Patented Sept. 5, 1967 when the zinc sulphate concentration in the bath is high, that is at or near 4 percent and, thus, the zinc in the viscose can be used to reduce the antagonistic action of zinc in the bath to the crimp in the fibre.
  • the second addition is that of relaxing the incompletely regenerated fibre in a dilute caustic soda solution. This has a remarkable elfect on the extensibility, causing increases of as much as 50 percent of the preexisting extensibility without deleteriously affecting the degree of crimp.
  • the relaxation of dried cellulose fibres in caustic soda solutions is a process which can only achieve increases of the order of 10 percent in the extensibility of the fibres, and the process is less efiicient than that of similarly treating the incompletely regenerated fibre.
  • the regeneration of the cellulose is more economically accomplished by continuing to treat the fibre with caustic soda, which hydrolyses the xanthate groups, rather than by reverting to an acid environment, in which the regeneration is due to the decay of free xanthic acid groups.
  • caustic soda which hydrolyses the xanthate groups
  • the change over from alkaline to acid conditions obviously involves the consumption of both acid and alkali.
  • the principle of alkaline regeneration is applicable in the manufacture of all kinds of viscose rayon fibres, but, in general, is useful only where an essential alkaline treatment follows the acid coagulation step.
  • the invention consists in extruding a viscose containing from 7.5 percent to 8.3 percent of cellulose, caustic soda such that the ratio of caustic soda to cellulose is between 0.7 and 0.9, 0.1 percent to 0.3 percent of polyethylene glycol having an average molecular weight of between 600 and 6,000 and a zinc compound in a proportion of from 0.04 percent to 0.2 percent of zinc based on the weight of the viscose, at a salt figure of from 5.5 to 8.5, into a coagulating and'regenerating bath containing sulphuric acid in a concentration of from 1.0 to 1.4 times the caustic soda content of the viscose, from 1 to 2 percent of zinc sulphate and between 22 and 24 percent of sodium sulphate, to form incompletely regenerated filaments, stretching the filaments by at least 60 percent of their original length in air, cutting the filaments into staple fibres and crimping the fibres by suspending the fibres in a solution containing between 1.5 and 2.5
  • Example 1 A viscose containing 8.3 percent of cellulose, 6.2 percent of caustic soda, 0.166 percent of polyethylene glycol having an average molecular weight of 1,500, and 0.22 percent of sodium zincate was extruded at a salt figure of 6 into a regenerating bath containing 7.8 percent of sulphuric acid, 24.0 percent of sodium sulphate and 1.8 percent of zinc sulphate.
  • the filaments so formed were withdrawn from the bath, stretched in air by 70 percent of their original length, cut into staple fibres and dropped into a solution containing 2 percent of caustic soda where they remained for 5 minutes. The fibres were then separated from the solution in a rotary extractor, washed, impregnated with acid, washed again, finished and dried.
  • a process for the production of crimped viscose rayon fibers comprising extruding a viscose containing from percent to percent of cellulose, from 5 percent to 10 percent of caustic soda, more than 0.05 percent of; a modifier and an alkali metal zincate in the proportion of from 0.01 percent to 0.8 percent of zinc based on the weight of the viscose, at a salt figure of between 3 and 14, into a coagulating and regenerating bath containing from 5 percent to 14 percent of sulphuric acid, from 0.5 percent to 4 percent of Zinc sulphate and more than 12 percent of sodium sulphate, to form incompletely regenerated filaments, stretching the filaments by at least 50 peIcent cutting the stretched filaments into staple fibres and crimping the fibres by relaxing the fibres in a solution containing between 1 percent and 5 percent of caustic soda, before completing the regeneration of the cellulose in the fibres.
  • a process comprising extruding a viscose contain ing from 7.5 percent to 8.3 percent ofcellulose, caustic soda such that the ratio of caustic soda to cellulose is between 0.7 and 0.9, 0.1 percent to 0.3 percent of polyethylene glycol having an average molecular weight of between 600 and 6,000 and an alkali metal zincate in a proportion of from 0.04 percent to 0.2 percent of zinc based on the Weight of the viscose, at a salt figurev of from 5.5 to 8.5, into a coagulating and regenerating bath containing sulphuric acid in a concentration of from 1.0 to 1.4 times the caustic soda content of the viscose, from 1 to 2 percent of zinc sulphate and between 22 and 24 percent of sodium sulphate, to form incompletely regenerated filaments, stretching the filaments by at least percent of their original length in air, cutting the filaments into staple fibres and crimping the fibres by suspending the fibres in a solution containing between 1.5 and 2.5 percent of ca

Landscapes

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

Description

United States Patent C) M 3,340,340 MANUFACTURE OF CRMPED VISCOSE RAYON FIBRES Ernest Mytum, Warwick, England, Assignor to Courtaulds Limited, London, England, a British company No Drawing. Filed Dec. 3, 1963, Ser. No. 327,818
Claims priority, application Great Britain, Dec. 11, 1962, 46,652/62 3 Claims. (Cl. 264-168) This invention is concerned with the manufacture of grilmped viscose rayon fibres having enhanced extensii 'ty.
United States patent specification No. 2,986,446 describes a process for the manufacture of crimped viscose rayon fibres by extruding a viscose containing polyethylene glycol into an acid coagulating and regenerating bath containing zinc sulphate, stretching the filaments so formed and relaxing the stretched filaments in an aqueous medium. The important properties of crimp and extensibility of the filament can be controlled by a change in one or more of the inherent features of the process, but, in general, a change which causes an increase in one property has the effect of decreasing the other. For example, the degree of crimp increases and the extensibility decreases when the filament is stretched more, whilst an increase in the zinc sulphate concentration in the bath increases the extensibility of the filament but decreases the degree of crimp. The properties of the filament can, therefore, be varied between high degree of crimp and low extension on the one hand and high extension and low degree of crimp on the other. The process is, however, incapable of producing a filament which combines the features of high degree of crimp and high extension.
Crimped staple fibres may be used as the pile of carpets. For this use, the fibres should be extensible, as this contributes to their resistance to abrasion, and resilient, to preserve the appearance of the carpet during wear. Viscose rayon fibres can be made more resilient by cross-linking the constituent cellulose, but this modification causes a decrease in extensibility. A viscose rayon fibre suitable for cross-linking and use in carpet piles, should, therefore, be highly extensible so as to be able to tolerate the inevitable fall in extensibility which accompanies crosslinking and still retain sufiicient extensibility to maintain the resistance to abrasion.
I have devised a process for the manufacture of crimped viscose rayon fibres having an increased extensibility.
According to the present invention a process for the production of crimped viscose rayon fibres comprises extruding a viscose containing from 5 percent to percent of cellulose, from 5 percent to 10 percent of caustic soda, more than 0.05 percent of a modifier and a zinc compound in the proportion of from 0.01 percent to 0.8 percent of zinc based on the weight of the viscose, at a salt figure of between 3 and 14, into a coagulating and regenerating bath containing from 5 percent to 14 percent of sulphuric acid, from 0.5 percent to 4 percent of zinc sulphate and more than 12 percent of sodium sulphate, to form incompletely regenerated filaments, stretching the filaments by at least 50 percent, cutting the stretched filaments into staple fibres and crimping the fibres by relaxing the fibres in a solution containing between 1 percent and 5 percent of caustic soda, before completing the regeneration of the cellulose in the fibres.
The increase in the extensibility of the fibre, is due, in the main, to two additions to the acknowledged, known process. The first of these is the use of a zinc compound, preferably an alkali metal zincate, in the viscose. This allows a desired degree of crimp to be obtained from a lower stretch, thus preserving to a greater extent the extensibility of the fibre. The effect is noticeable even 3,340,340 Patented Sept. 5, 1967 when the zinc sulphate concentration in the bath is high, that is at or near 4 percent and, thus, the zinc in the viscose can be used to reduce the antagonistic action of zinc in the bath to the crimp in the fibre.
The second addition is that of relaxing the incompletely regenerated fibre in a dilute caustic soda solution. This has a remarkable elfect on the extensibility, causing increases of as much as 50 percent of the preexisting extensibility without deleteriously affecting the degree of crimp. The relaxation of dried cellulose fibres in caustic soda solutions is a process which can only achieve increases of the order of 10 percent in the extensibility of the fibres, and the process is less efiicient than that of similarly treating the incompletely regenerated fibre.
Once the incompletely regenerated fibre has been rendered alkaline in the relaxing step, the regeneration of the cellulose is more economically accomplished by continuing to treat the fibre with caustic soda, which hydrolyses the xanthate groups, rather than by reverting to an acid environment, in which the regeneration is due to the decay of free xanthic acid groups. The change over from alkaline to acid conditions obviously involves the consumption of both acid and alkali. The principle of alkaline regeneration is applicable in the manufacture of all kinds of viscose rayon fibres, but, in general, is useful only where an essential alkaline treatment follows the acid coagulation step.
In a preferred form, the invention consists in extruding a viscose containing from 7.5 percent to 8.3 percent of cellulose, caustic soda such that the ratio of caustic soda to cellulose is between 0.7 and 0.9, 0.1 percent to 0.3 percent of polyethylene glycol having an average molecular weight of between 600 and 6,000 and a zinc compound in a proportion of from 0.04 percent to 0.2 percent of zinc based on the weight of the viscose, at a salt figure of from 5.5 to 8.5, into a coagulating and'regenerating bath containing sulphuric acid in a concentration of from 1.0 to 1.4 times the caustic soda content of the viscose, from 1 to 2 percent of zinc sulphate and between 22 and 24 percent of sodium sulphate, to form incompletely regenerated filaments, stretching the filaments by at least 60 percent of their original length in air, cutting the filaments into staple fibres and crimping the fibres by suspending the fibres in a solution containing between 1.5 and 2.5 percent of caustic soda, before completely regenerating the fibres.
The invention is illustrated by the following example in which percentages are by weight.
Example 1 A viscose containing 8.3 percent of cellulose, 6.2 percent of caustic soda, 0.166 percent of polyethylene glycol having an average molecular weight of 1,500, and 0.22 percent of sodium zincate was extruded at a salt figure of 6 into a regenerating bath containing 7.8 percent of sulphuric acid, 24.0 percent of sodium sulphate and 1.8 percent of zinc sulphate. The filaments so formed were withdrawn from the bath, stretched in air by 70 percent of their original length, cut into staple fibres and dropped into a solution containing 2 percent of caustic soda where they remained for 5 minutes. The fibres were then separated from the solution in a rotary extractor, washed, impregnated with acid, washed again, finished and dried.
The corresponding properties of a fibre produced by the process from which the caustic soda relaxation was omitted, were:
Air dry tenacity g./d 2.32 Air dry extensibility percent 25.3 Wet tenacity g./d 1.23 Wet extensibility percent 35.2 Waves/cm. 2.7
and when this fully regenerated fibre was treated with 2 percent caustic soda, washed and dried, the properties became:
1. A process for the production of crimped viscose rayon fibers comprising extruding a viscose containing from percent to percent of cellulose, from 5 percent to 10 percent of caustic soda, more than 0.05 percent of; a modifier and an alkali metal zincate in the proportion of from 0.01 percent to 0.8 percent of zinc based on the weight of the viscose, at a salt figure of between 3 and 14, into a coagulating and regenerating bath containing from 5 percent to 14 percent of sulphuric acid, from 0.5 percent to 4 percent of Zinc sulphate and more than 12 percent of sodium sulphate, to form incompletely regenerated filaments, stretching the filaments by at least 50 peIcent cutting the stretched filaments into staple fibres and crimping the fibres by relaxing the fibres in a solution containing between 1 percent and 5 percent of caustic soda, before completing the regeneration of the cellulose in the fibres.
2. A process comprising extruding a viscose contain ing from 7.5 percent to 8.3 percent ofcellulose, caustic soda such that the ratio of caustic soda to cellulose is between 0.7 and 0.9, 0.1 percent to 0.3 percent of polyethylene glycol having an average molecular weight of between 600 and 6,000 and an alkali metal zincate in a proportion of from 0.04 percent to 0.2 percent of zinc based on the Weight of the viscose, at a salt figurev of from 5.5 to 8.5, into a coagulating and regenerating bath containing sulphuric acid in a concentration of from 1.0 to 1.4 times the caustic soda content of the viscose, from 1 to 2 percent of zinc sulphate and between 22 and 24 percent of sodium sulphate, to form incompletely regenerated filaments, stretching the filaments by at least percent of their original length in air, cutting the filaments into staple fibres and crimping the fibres by suspending the fibres in a solution containing between 1.5 and 2.5 percent of caustic soda, before completely regeneratin g the fibres.
3. A process as claimed in claim 2 in which the cellulose in the fibres is completely regenerated by contact with a caustic soda solution.
References Cited UNITED STATES PATENTS 2,515,834 7/1950 Nicoll 264168 X 2,860,480 11/1958 Cox 264197 X 2,879,170 3/1959 Miller l06165 X 2,966,391 12/1960 Bandel 264197 X 2,986,446 5/1961 Smith 264198 X 3,046,083 7/ 1962 Baites et a1. 264-168 FOREIGN PATENTS 570,159 6/1945 Great Britain.
ALEXANDER H. BRODMERKEL, Primary Examiner.
J. H. WOO, Assistant Examiner.

Claims (1)

1. A PROCESS FOR THE PRODUCTION OF CRIMPED VISCOSE RAYON FIBERS COMPRISING EXTRUDING A VISCOSE CONTAINING FROM 5 PERCENT TO 10 PERCENT OF CELLULOSE, FROM 5 PERCENT TO 10 PERCENT OF CAUSTIC SODA, MORE THAN 0.05 PERCENT OF A MODIFIER AND AN ALKALI METAL ZINCATE IN THE PROPORTION OF FROM 0.01 PERCENT TO 0.8 PERCENT OF ZINC BASED ON THE WEIGHT OF THE VISCOSE, AT A SALT FIGURE OF BETWEEN 3 AND 14, INTO A COAGULATING AND REGENERATING BATH CONTAINING FROM 5 PERCENT TO 14 PERCENT OF SULPHURIC ACID, FROM 0.5 PERCENT TO 4 PERCENT OF ZINC SULPHATE AND MORE THAN 12 PERCENT OF SODIUM SULPHATE, TO FORM INCOMPLETELY REGENERATED FILAMENTS, STRETCHING THE FILAMENTS BY AT LEAST 50 PERCENT, CUTTING THE STRETCHED FILAMENTS INTO STAPLE FIBRES AND CRIMPING THE FIBRES BY RELAXING THE FIBRES IN A SOLUTION CONTAINING BETWEEN 1 PERCENT AND 5 PERCENT OF CAUSTIC SODA, BEFORE COMPLETING THE REGENERATION OF THE CELLULOSE IN THE FIBRES.
US327818A 1962-12-11 1963-12-03 Manufacture of crimped viscose rayon fibres Expired - Lifetime US3340340A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB46652/62A GB1060311A (en) 1962-12-11 1962-12-11 Improvements in and relating to the manufacture of crimped viscose rayon fibres

Publications (1)

Publication Number Publication Date
US3340340A true US3340340A (en) 1967-09-05

Family

ID=10442074

Family Applications (1)

Application Number Title Priority Date Filing Date
US327818A Expired - Lifetime US3340340A (en) 1962-12-11 1963-12-03 Manufacture of crimped viscose rayon fibres

Country Status (6)

Country Link
US (1) US3340340A (en)
AT (1) AT250553B (en)
BE (1) BE641106A (en)
DE (1) DE1234917B (en)
GB (1) GB1060311A (en)
NL (1) NL301646A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3423499A (en) * 1965-02-18 1969-01-21 Fmc Corp Process for spinning modified xanthated polymers
US3632468A (en) * 1968-04-09 1972-01-04 Rayonier Inc High-crimp, high-strength rayon filaments and staple fibers and process for making same
US4051300A (en) * 1973-09-03 1977-09-27 Gulf South Research Institute Hollow synthetic fibers
EP0207721A2 (en) 1985-06-27 1987-01-07 A/G Technology Corporation Anisotropic membranes for gas separation

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB570159A (en) * 1943-11-18 1945-06-25 Courtaulds Ltd Improvements in and relating to the production of crimped artificial threads by the viscose process
US2515834A (en) * 1942-11-13 1950-07-18 Du Pont Cellulose filaments and method of producing same
US2860480A (en) * 1956-04-18 1958-11-18 Du Pont Regenerated cellulose structures and process for producing them
US2879170A (en) * 1957-10-02 1959-03-24 Du Pont Chemical composition and process
US2966391A (en) * 1955-10-12 1960-12-27 Spinnfaser Ag Manufacture of regenerated cellulose fibers
US2986446A (en) * 1956-08-01 1961-05-30 Courtaulds Ltd Crimped regenerated cellulose fibres
US3046083A (en) * 1960-06-06 1962-07-24 American Viscose Corp Method for producing crimped rayon staple fiber

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2515834A (en) * 1942-11-13 1950-07-18 Du Pont Cellulose filaments and method of producing same
GB570159A (en) * 1943-11-18 1945-06-25 Courtaulds Ltd Improvements in and relating to the production of crimped artificial threads by the viscose process
US2966391A (en) * 1955-10-12 1960-12-27 Spinnfaser Ag Manufacture of regenerated cellulose fibers
US2860480A (en) * 1956-04-18 1958-11-18 Du Pont Regenerated cellulose structures and process for producing them
US2986446A (en) * 1956-08-01 1961-05-30 Courtaulds Ltd Crimped regenerated cellulose fibres
US2879170A (en) * 1957-10-02 1959-03-24 Du Pont Chemical composition and process
US3046083A (en) * 1960-06-06 1962-07-24 American Viscose Corp Method for producing crimped rayon staple fiber

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3423499A (en) * 1965-02-18 1969-01-21 Fmc Corp Process for spinning modified xanthated polymers
US3632468A (en) * 1968-04-09 1972-01-04 Rayonier Inc High-crimp, high-strength rayon filaments and staple fibers and process for making same
US4051300A (en) * 1973-09-03 1977-09-27 Gulf South Research Institute Hollow synthetic fibers
EP0207721A2 (en) 1985-06-27 1987-01-07 A/G Technology Corporation Anisotropic membranes for gas separation

Also Published As

Publication number Publication date
BE641106A (en) 1964-06-11
DE1234917B (en) 1967-02-23
NL301646A (en)
AT250553B (en) 1966-11-25
GB1060311A (en) 1967-03-01

Similar Documents

Publication Publication Date Title
US2705184A (en) Process for the production of rayon products
US1989099A (en) Process of improving artificial threads
US3720743A (en) Process for producing high performance crimped rayon staple fiber
US3626045A (en) Process for making tubular filaments
US2439813A (en) Artificial filament
US3758458A (en) Low d p high d p viscose mixture using high cellulose concentration
US3340340A (en) Manufacture of crimped viscose rayon fibres
US3337671A (en) Method of making regenerated cellulose filaments
US2997365A (en) Production of regenerated cellulose filaments
US3352957A (en) Process for spinning cellulosic fibers
US3226461A (en) Manufacture of regenerated cellulose fibers from viscose
US3108849A (en) Process for producing viscose regenerated cellulose fibers
US3146116A (en) Cyanoethylation and xanthation of alkali cellulose
US3419652A (en) Process for producing highly crimped fibers
US3539679A (en) Process for producing polynosic fibers
US2975023A (en) Production of regenerated cellulose filaments
GB1002621A (en) Regenerated cellulose filaments and staple fibers and their production
US2328307A (en) Manufacture of rayon
US3097914A (en) Process for the production of a ribbon filament yarn of regenerated cellulose
US2439039A (en) Process of producing medullated artificial filaments
US2114915A (en) Process of spinning rayon and the bath used
US2792280A (en) Viscose composition and method of spinning
US3109699A (en) Method for making rayon filaments
US3077374A (en) Method for producing crimped regenerated cellulosic fibers
US3116353A (en) Spinning viscose