US2505033A - Method of producing high tenacity regenerated cellulose yarns - Google Patents

Method of producing high tenacity regenerated cellulose yarns Download PDF

Info

Publication number
US2505033A
US2505033A US591382A US59138245A US2505033A US 2505033 A US2505033 A US 2505033A US 591382 A US591382 A US 591382A US 59138245 A US59138245 A US 59138245A US 2505033 A US2505033 A US 2505033A
Authority
US
United States
Prior art keywords
yarns
saponification
cellulose
yarn
stretched
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
US591382A
Inventor
William J Elvin
John B Steiding
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.)
Celanese Corp
Original Assignee
Celanese Corp
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 Celanese Corp filed Critical Celanese Corp
Priority to US591382A priority Critical patent/US2505033A/en
Application granted granted Critical
Publication of US2505033A publication Critical patent/US2505033A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating 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
    • D06M11/32Treating 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
    • D06M11/36Treating 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
    • D06M11/38Oxides or hydroxides of elements of Groups 1 or 11 of the Periodic System
    • D06M11/385Saponification of cellulose-acetate
    • 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
    • D01F2/24Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from cellulose derivatives
    • D01F2/28Monocomponent 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

Landscapes

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

Description

April25, 1950 w. J. ELVIN ETAL 2,505,033
METHOD 0F PRODUCING HIGH-TENACITY REGENERATED CELLULOSE YARNS Filed May 1. 1945- IN V EN TORS 'WILLIAMJ. ELVIN. B JOHN B. STEIDING.
Y wi j m ATTORNEYS.
Patented Apr. 25, 1950 METHOD OF PRODUCING HIGH TENACITY BEGENERATED CELLULOSE YARNS I William J. Elvin, Frostburg, and John B. Steiding,
Midland, Md., assignors to Celanese Crpora-. tion of America, a corporation of Delaware.
Application May 1, 1945, Serial No. 591,382; 7
4 Claims. (01. 81-130) This invention relates to the preparation of high tenacity regenerated cellulose yarns, and relates more particularly to improved saponification methods for the production of said high tenacity regenerated cellulose yarns from stretched yarns having a basis of cellulose acetate, or other or-. ganic ester of cellulose.
An object of this invention of regenerated cellulose yarns of higher tenacities by a process involving the saponification of stretched yarns having a basis of cellulose acetate or other organic ester of cellulose.
Another object of this invention is the pro-. vision of an improved saponification processior the production of said regenerated cellulose yarns from stretched yarns of cellulose acetate or other organic ester of cellulose wherein higher yarn tenacities with lim ted weight loss of the -saponi-' fied yarns are obtained.
A further object of this invention is the provision of improved apparatus for the continuous, saponification of yarns, and more especially, stretched yarns having a basis of cellulose acetate or other organic ester of cellulose, wherein means are provided for controlling the tension exerted thereon.
Other objects of this invention will appear'from the following detailed description and the accompanying drawing.
In the drawing, wherein a preferred embodiment of our novel apparatus for carrying out our invention is shown,
Fig. 1 is a plan view of an improved apparatus" for the continuous, controlled saponification of cellulose acetate or other organic ester of cellulose yarns, v
Fig. 2 is a side elevational view, partly in section, of this apparatus showing th roller system in askewed relation, and
Fig. 3 is a plan View, onan enlarged scale of one of the rollers employed in our novel continuous saponification apparatus. i e
Like reference numerals indicate like parts throughout the several views of the drawing.
Yarns of regenerated cellulose of high tenacity have been produced by the saponification of stretched yarns having a basis of an organic esterof cellulose, such as, for example,"cellulose ace tate. The stretching of the yarns is effected dur-' ing' some stage in'their manufacture and the yarns may be increased in length as a" result-of the stretching operation to the extent of 200, 300, 500, or even 1000 or 2000% of their original length. The yarns acquire a" relatively high tenacity on bein stretched, the tenacity being retainedzand inman y instances enhanced by saponification' is the preparation which, as is well known, effects a regeneration. .of the cellulose. Theresulting high tenacity re-' generated cellulose yarns are of great strength and find extensive employment where yarns of an unusual degree of strength and dimensional.
stability are desired.
During the saponiflcation of the stretched cel-. lulose acetate or other. organic ester of cellulose yarns, the latter undergov various physical and chemcal changes. One important physical change which the stretched cellulose acetate.
yarns undergoduring saponification is an increase in length at the start of saponification due to linear as well as lateral swelling of the yarns as they are wet out followed by marked linear shrinkage involving an appreciable decrease in length. The shrinkage varies depending upon the nature of the stretched. product undergoing saponification. A considerable loss in the weight of the cellulose acetate yarns also takes place due to the fact that the acetyl groups present are split oiT by the saponifyin agent employed. Moreover, this chemical change causes the yarns to undergo a pronounced decrease in denier which, because the breaking. load is usually retained, produces yarnslof substantially increased.
tenacity. An additionalweight loss also takes place by reason of the factthat certain alkali-,
soluble fractions of the regenerated cellulose produced are removed as .well, Such weight and shrinkage losses decrease the yield of regenerated cellulose yarn which may be obtained from a given quantity of stretched cellulose acetate yarns which decreaseis, of course. undesirable. 7 We have now discoveredthat regenerated cellulose yarnsof superior physical characteristics may be obtained with a minimum weight loss by an improved saponification process. In accordance with our novel saponification process, the stretched cellulose acetate or other organic ester of cellulose yarns are saponified under a predeterm ned and controlled tension so that the ultimate shrinkage effected during saponification is held Within predetermined limits, whereby the shrinkage effected as a result of the saponification reaction is less than that normally produced when such'yarns are saponified in a relaxed condition, e; g. in the absence of tension, and allowed to shrink freely. Surprisingly enough, this novel methodof saponifying cellulose acetate "or other organic ester of cellulose yarns, wherein the yarns are maintained under controlled tensionjduring saponification, vproduces substantially completely regenerated cellulose yarns of an even higher jtenacity then-are normally obtained with the same cellulose acetate yarns, but saponified in the saponifying bath and that the retention of 3 these cellulosic fractions in theregeneratedrceb lulose yarns obtained is responsible ;.for thejimproved pliability and softnesspossessed by the yarns obtained in accordance with our process. This explanation, however, is merelyatheoretical one and we do not wish to be bound'thereby.
The desired degree of control:over theshrink age of the cellulose acetate yarns is achieved by maintaining the yarns under predetermined tension during the progress of the saponification re action, which tension maybe obtained in any convenient manner. Thus, 'for example, the yarns may besaponifie'din a continuous manner while passing from one yarn guide to another in the saponifyingbathemployed, the yarnguides being spring loaded or otherwise adapted to maintain theyarnsunder'thedesired degree of tension at each stage of the sapon'ification.
"Preferably, however, the yarns undergoing saponificationtare maintained under thedesired. controlled tension. by being passed continuously from one driven roller to another, partially or wholly submerged'in thed'esired saponifying bath. Tothis end we employ'a novel apparatus comprising a plurality of rollers the contour of which is such asto permit: some shinkage of the yarns to take place during the saponification process, but at thesame time, to maintain the yarns under a continuous :and predeterminedamount of tension at each stage of the saponification operation, whereby the total degree of shrinkage taking place is limited, and is less than that effected when.
theyarnsare saponifled in a completely relaxed condition.
of yarn 5 across the sections of rollers i5 and I generally indicated by the letter A. The sections A are of gradually increasing diameter, and thereact to take up any increase in the length due to relaxation of the yarn. As the saponiiy action of bath l begins to effect yarn 5, the lat e gradually begins to shrink. The rollers 7e and however, are rotated at such speed in timed relation to the rate of saponification that w...en this phase of the saponification is reached the yarn 5 is passing oversection B of said rollers. This section is n-ottapered but is substantially cylindrical in form since while passin over section jB therateofshrinkage is not sufficient to r quire .a changein the, contour of the roller to eliminate the excessive development of tension due to shrinkage. iI-Iowever, since the yarn continues to shrinkasit undergoes further saponification, increasing degree of tension is placed upon the yarn due to the unyielding rollers. Accordingly, as saponification proceeds further, the yarn undergoing saponification gradually moves .in a lateral direction across the contoured rollers 6 and i, still in timed relationship'to the degree of saponificaticaand finally reaches section C of said rollers which section is provided with a suitable taper. The taper of section C is such that it enables the yarn. to shrink but at the same time maintains it under-the desired tension. The contour of section 0 is such as to compensate 'for a grad ually increasing rate of shrinkage and'thi revents the tension on the yarn from building up to an undesirably high level. The 'substait' completely sapcnified yarn leaving roller '5 may be washed, neutralized'and dried in a continuous manner, or the yarn may be'taken up in the form of a suitablepackage and the yarn maybe new tralized, washed and'dried in. package form. Bur
. ing drying, the yarn may be allowed'to mini;
the greater will be the degree of shrinkage ef- Referringnow' to the drawing, astretched ceilulose acetate .yarn 5 coming "from a suitable sourceof supply (notshown) is passed, as .many times asdesired, around a pair of identical rollers 6. and. l .mounted-on shafts .8 and ,9 respectively, the shaft .9 fcarryingroller lgbeing somewhat askewwith respect .to shaft 8.. .The rollers iend IV are ,shownaon. asomew-hat enlargedscale .inJiig. 3. Shafts-8 and Son whichthe rollers are mounted-are provided withrsuitable drivingmeans not shown) so that they maybe driven at any -desired speed, thus continuously advancing :yarn 5 through the-:bath. Themethod of mounting shafts 3 and 9 so; that. shaftx9.-.-is-notparallel vtc shaft lL-gives alead to-the-yarnpassing around said rollers and not only @keepsthe ,yarn wraps apart :but also causes yarn :5 to move laterally alongthe surface of the rollers. Rollers 6 and l are partially submerged in a saponifying bath l5 ofany suitable composition whichiis contained inatroughil Asstated, the rollers 5 and! may, ifidesiredyalso be wholly-submerged in bath ii thus'maintaining the'cellulose-acetate yarn 5 in constant contact with-the saponifying bath 0.
towet out yarn 5. "This' actionttends 'totrelax the stretched yarn-5.'somewhat,'permittingit to in the yarn to compensateffor'anyincrease inlength.
This' take-np is effected by the lateral-movement fected during drying.
The tensions under which theyarns aremaintained during thestages of the saponification operation whereby -the degree of shrinkage they undergo is limited, may be irom'0.02 to 05 gram per denier'but optimum results are achieved when aqueous-alcoholic. solutions. :Advantageously, the
hydroxide are employed as the saponifying agent, the sodium hydroxide may be presentin.
a, concentration of from 0.lto 5% by weight and saponification may-beefiected in-from 1 to 69 minutes: with" the solution; at a temperature of from '30;to C. whenemploying aqueous solutions :of sodium hydroxide; as the saponityingg medium, it is preferable to include a salt such as sodium sulfate or sodium acetate in said solution.
To eifect the desired saponiflcation the stretched yarns are led directly into the saponifying bath, the path through the saponiiying bath being sufficiently extended and the speed at which the yarns pass'through thebath being such that the yarn, under the conditions of both" temperature and concentration employed,- is
completely saponified before leaving the; bath-L Speeds of 10 to 100 meters per minute are satisfactory.
'While our invention hasbeen more particularly described in connection with con'tiriiious saponiflcation processes, batch processes "may tension.
In order further to illustrate our invention but without" being limited thereto the following example is given:-
Example A 144 denier, 12o filament celluloseacetate yarn, which has been prepared by subjecting a d 1440 denier yarn to a 10 times stretch, is saponifled in a continuous manner at 80 C..with a saponifying bath comprising a 0.7% aqueous solution of sodium hydroxide containing 8.5% by. weight of sodium. acetate. The yarns are passed through the saponifying bath at a speed of 10 meters per minute and the path of the yarn is of. such extent that itissubjected to the action of the saponifying bath for 11 minutes. During sa oniflcation the yarns passing through the bath are maintained under a continuous tension in the manner heretofore described,-employing a pair of driven, novel contoured rollers around which the running yarn ispassed. The initial taper of the rollers is such that as the yarn pa ses into the bath it is placed under tension with the taper of the rollers extending the yarn path to avoid the formation of any slack; because of the relaxing or swelling effect of the initial wetting. The slackening permits the yarn to increase about 0.35% in length which 15.01: course, taken up the increasing diameter of the contoured rollers. The tension under which the yarn is maintained amounts to about 0.03' ram per denier. The loops are then led across the tapered rollers in timed relation to the shrinkage and to the saponiflcation. The contour of the rollers is such that the yarns are also maintained under a substantially uniform tension of 0.03 gram per denier during the initial saponiflcation across the flat portion of the rollers as well as during the latter stage of saponiflcation across the final tapered portion. The degree oi. shrinkage permitted by maintaining the yarns under tension is thereby limited to about 0.35% of the original yarn length, a total change in length of 0.70% taking place when determined from the initial, relaxed state. The saponified, regenerated cellulose yarns obtained are washed, neutralized with a 1% aqueous solution of acetic acid, washed and dried at 80 C. to a moisture content of 0.75%. The regenerated cellulose yarn produced is of about 100 denier, has a dry tenacity of 7.3 grams per denier and a wet tenacity of 6.5 grams per denier. The over-all linear shrinkage of the yarn from its original length is found to be only 0.9%, a shrinkage of 0.55% having occurred during drying to the particular moisture content inlike saponiflcation, said yarn shrinks about 0.55% T in length due to the saponiflcation and a total of 1.45% when dried to a like moisture content, a shrinkage of 0.9% taking place as a result of drying. The weight loss of the yarns saponified under tension in accordance with our novel process amounts to about 37.5% while the weight loss for like cellulose acetate yarns saponified under the same conditions but in a relaxed state amounts to about 40%.
The cellulose acetate or other organic ester of cellulose yarns which may be stretched and then saponified in accordance with our novel process toyield regenerated cellulose yarns of improved tenacity may be prepared by extruding a solution of cellulose acetate or other organic ester of cellulose dissolved in a suitable volatile solvent, through a plurality of orifices into an evaporative medium as in the dry method of spinning, or into a coagulating or precipitating liouid medium as in the wet method of spinning. The filaments formed in this manner are associated together to form the desired multi-filament yarn or thread which is, first stretched and then saponified.- In addition to cellulose acetate, other organic esters of cellulose which may be employed for the preparation of the yarns are, for example, cellulose propionate, cellulose butyrate, and mixed esters such as, cellulose acetate-propionate and cellulose acetate-butyrate.
The cellulose acetate or other organic ester of cellulose employed may be of any degree of esterification. For example, in the case of cellulose. acetate materials, they may have an acetyl value of from 40 to 62%, calculated as acetic acid.
After the yarn or thread is formed, it is then stretched. This is usually done when the yarn is in a somewhat softened condition. The yarn may be so tened by trea ing it with a solvent,
; latent solvent. or swelling agent for the cellu ose or padding methods, or b exposing the celluloseacetate materia s to vapors of said organic solvents, latents solvents or swelling agents during, or just prior to. the stretching operation. The yarns ma a so be softened by radiant heat or by the use of steam or hot water. After softening, the yarns may be stretched in a continuous manner by being passed from a roll which rotates at a slow speed to one rotating at a higher speed, the ro ler rotating at a h gher s eed serving to give the yarn the desired stretch. The de ree of stretch ma be vari d by increasing or decreasing J the differential in the speeds of the rollers. The
yarn may be stretched in a p urality of sta es, if desired. For example, part of the stretch may be imparted to the yarn by softening and stretching in one sta e and the remainder of the stretch may be imparted by a second softening and stretching operation, but more than two s ages of stretch may, of course, be emplo ed. A ter s retching the yarns ma be taken up on bob ins or ma be collected in a centrifugal spinning box or Topham box and are ready for saponiflcation in accordance with our novel process.
It is to be understood that the foregoing detailed description is given merely by way of illustrat on and that many variations may be made therein without departing from the spirit of our invention.
Having described our invention, what we desire to secure by Letters Patent is:
1. In a process for the production of improved dicated. When allowed to shrink freely during high tenacity regenerated cellulose yarns by the saponification of :str-etched yarns having -a basis of an organic ester 70fv cellulose, wherein-the yarns undergoing saponification increase in length :and then 'decrease :in length :as said rsaponification proceeds, the step which scomprlsescontinuously feeding said organicester-ofecellulose yarns into a' saponifyingbathand placing the -wetted yarns under a controlled and predetermined-tension.of 0.02 to 0.5 gram 'persden-ier' in the saponifying bath throughout the entire asaponificatmn ,process, whereby the degree of shrinkage eflected-by the saponification reaction-is limitedto vlessithan that-reflected when said yarns are.saponifiedina substantially untensionedrcondition.
2. In -aprocess for ,thelproduction.oflimproved high tenacityregenerated;cellulose.yarns by the saponification of stretchedyarns havinga basis of celluloseacetate, wherein they-ems undergoing saponification increase .in -length .and .then. decrease in-length as said saponiflcatlonproceeds,-
the step "which comprises continuously .feeding said celiulose acetate yarns .into vawsaponifying bath and placing :the @wetted yarns :under .a controlled and predetermined tens-ion.of 0.02 to 0.5 gram per denier in'the saponifying bath throughout-the entire saponificationiprocess, Wherebylthe degree of shrinkage .efiected Joy-the saponification-reaction is limited toless than that effected when said yarns are saponified in a substantially untensioned condition.
.3. In a process for the productionof improved high tenacityregenerated celluloseyarns by the saponification of" stretched ,yarnshaving a, basis of celluloseaacetate, wherein the yarns undergoing saponificationlincrease inlength and then decrease in --length as said saponification proceeds, the step which comprises continuously feeding said cellulose acetate yarns into alsaponifying.
bath comprising an aqueous alkaline medium and placing the wetted yarns-under a controlled and predetermined --tension of-0.02 to 0.5 gram per denier in the saponifying bath throughout .the entire-saponification process, whereby thedegree 0f'-.shrinkage effected by thesaponificationlreactionis li-mitedtoless than that effected whensaid yarns are saponified in a substantially untensioned condition.
.4. In a process-for the production of improved hightenacity. regenerated cellulose yarns "by-the saponification :of stretched yarnshaving a basis of cellulose acetate, wherein the yarns undergoing saponificationincrease in.-1ength--and=then decrease in length as-said saponification proceeds, the step which comprises continuously ifeeding said cellulose {acetate yarnsinto -a saponifying bath comprising an aqueous solution of sodium hydroxide and placing the wetted yarns under: a controlled and predetermined tension of 0.02 :to 0.5 gram per denier :in the saponifying bath throughout the *entire saponification process, whereby the degree. of shrinkage efiected by-the saponification reaction. is limited to less than that efiected when said yarns are seponified in asubstantiall-y untensioned condition.
WILLIAM- J. ELVIN. JOHN B.-SEI-EIDING.
REFERENCES CITED The following-references are-of record in the fileof .this patent:
UNITED STATES PATENTS

Claims (1)

1. IN A PROCESS FOR THE PRODUCTION OF IMPROVED HIGH TENACITY REGENERATED CELLULOSE YARNS BY THE SAPONIFICATION OF STRETCHED YARNS HAVING A BASIS OF AN ORGANIC ESTER OF CELLULOSE, WHEREIN THE YARNS UNDERGOING SAPONIFICATION INCREASE IN LENGTH AND THEN DECREASE IN LENGTH AS SAID SAPONIFICATION PROCEEDS, THE STEP WHICH COMPRISES CONTINUOUSLY FEEDING SAID ORGANIC ESTER OF CELLULOSE YARNS INTO A SAPONIFYING BATH AND PLACING THE WETTED YARNS UNDER A CONTROLLED AND PREDETERMINED TENSION OF 0.02 TO 0.5 GRAM PER DENIER IN THE SAPONIFYING BATH THROUGHOUT THE ENTIRE SAPONIFICATION PROCESS, WHEREBY THE DEGREE OF SHRINKAGE EFFECTED BY THE SAPONIFICATION REACTION IS LIMITED TO LESS THAN THAT EFFECTED WHEN SAID YARNS ARE SAPONIFIED IN A SUBSTANTIALLY UNTENSIONED CONDITION.
US591382A 1945-05-01 1945-05-01 Method of producing high tenacity regenerated cellulose yarns Expired - Lifetime US2505033A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US591382A US2505033A (en) 1945-05-01 1945-05-01 Method of producing high tenacity regenerated cellulose yarns

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US591382A US2505033A (en) 1945-05-01 1945-05-01 Method of producing high tenacity regenerated cellulose yarns

Publications (1)

Publication Number Publication Date
US2505033A true US2505033A (en) 1950-04-25

Family

ID=24366270

Family Applications (1)

Application Number Title Priority Date Filing Date
US591382A Expired - Lifetime US2505033A (en) 1945-05-01 1945-05-01 Method of producing high tenacity regenerated cellulose yarns

Country Status (1)

Country Link
US (1) US2505033A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2694912A (en) * 1948-09-02 1954-11-23 American Viscose Corp Apparatus for the liquid treatment of running filamentary materials
US2718136A (en) * 1952-10-30 1955-09-20 American Viscose Corp Lacing guide for yarn treating apparatus
US2721466A (en) * 1952-01-15 1955-10-25 American Viscose Corp Apparatus for the countercurrent liquid treatment of yarn
US2851043A (en) * 1954-05-24 1958-09-09 Us Rubber Co Apparatus for washing rubber threads
US2897577A (en) * 1954-05-12 1959-08-04 Grove Silk Company Method of dulling nylon and like materials
EP1272694A1 (en) * 2000-03-27 2003-01-08 SK Chemicals Co., Ltd. Cellulosic materials having composite crystalline structure
US20050082130A1 (en) * 2003-10-17 2005-04-21 Mcgrath Donnie Device for transporting large planar rollable objects

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB415412A (en) * 1933-02-20 1934-08-20 Henry Dreyfus Improvements in the manufacture of treatment of artificial filaments, threads, yarns, ribbons, fabrics and the like made from or containing organic esters of cellulose
US2002996A (en) * 1932-03-05 1935-05-28 American Bemberg Corp Continue process and apparatus
GB435806A (en) * 1934-03-27 1935-09-27 British Celanese Improvements in the saponification of cellulose ester filaments, threads, fabrics, films and the like
US2090064A (en) * 1935-10-05 1937-08-17 Tubize Chatillon Corp Spinning apparatus
US2092007A (en) * 1933-12-12 1937-09-07 Celanese Corp Treatment or manufacture of cellulose ester material
US2107451A (en) * 1935-09-28 1938-02-08 Tubize Chatillon Corp Manufacture of rayon and the like
US2142909A (en) * 1934-05-30 1939-01-03 Celanese Corp Treatment of artificial materials
US2142910A (en) * 1934-05-30 1939-01-03 Celanese Corp Apparatus for the manufacture of artificial materials
GB509854A (en) * 1939-02-24 1939-07-24 Lustrafil Ltd Improvements in or relating to the treatment of filaments, threads or yarns

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2002996A (en) * 1932-03-05 1935-05-28 American Bemberg Corp Continue process and apparatus
GB415412A (en) * 1933-02-20 1934-08-20 Henry Dreyfus Improvements in the manufacture of treatment of artificial filaments, threads, yarns, ribbons, fabrics and the like made from or containing organic esters of cellulose
US2092007A (en) * 1933-12-12 1937-09-07 Celanese Corp Treatment or manufacture of cellulose ester material
GB435806A (en) * 1934-03-27 1935-09-27 British Celanese Improvements in the saponification of cellulose ester filaments, threads, fabrics, films and the like
US2142909A (en) * 1934-05-30 1939-01-03 Celanese Corp Treatment of artificial materials
US2142910A (en) * 1934-05-30 1939-01-03 Celanese Corp Apparatus for the manufacture of artificial materials
US2107451A (en) * 1935-09-28 1938-02-08 Tubize Chatillon Corp Manufacture of rayon and the like
US2090064A (en) * 1935-10-05 1937-08-17 Tubize Chatillon Corp Spinning apparatus
GB509854A (en) * 1939-02-24 1939-07-24 Lustrafil Ltd Improvements in or relating to the treatment of filaments, threads or yarns

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2694912A (en) * 1948-09-02 1954-11-23 American Viscose Corp Apparatus for the liquid treatment of running filamentary materials
US2721466A (en) * 1952-01-15 1955-10-25 American Viscose Corp Apparatus for the countercurrent liquid treatment of yarn
US2718136A (en) * 1952-10-30 1955-09-20 American Viscose Corp Lacing guide for yarn treating apparatus
US2897577A (en) * 1954-05-12 1959-08-04 Grove Silk Company Method of dulling nylon and like materials
US2851043A (en) * 1954-05-24 1958-09-09 Us Rubber Co Apparatus for washing rubber threads
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
US20050082130A1 (en) * 2003-10-17 2005-04-21 Mcgrath Donnie Device for transporting large planar rollable objects

Similar Documents

Publication Publication Date Title
US2505033A (en) Method of producing high tenacity regenerated cellulose yarns
US2772944A (en) Process for the acetylation of regenerated cellulose fibers and product resulting therefrom
US2070584A (en) Production and treatment of artificial filaments, threads, ribbons, and the like
US2147642A (en) Production of artificial filaments, films, and like materials
US2702230A (en) Cellulose acetate spinning process
US2552598A (en) Production of cellulose ester textile materials
US2385403A (en) Method for stretching cellulose ester yarn
US2439829A (en) Method of producing artificial yarn
US2075027A (en) Manufacture and treatment of artificial silk and like products
US1914491A (en) Textile material and method of making the same
US2147641A (en) Production of artificial filaments, films, and like materials
US2039306A (en) Manufacture and treatment of artificial silk and the like
US2116063A (en) Treatment of artificial materials
US2072250A (en) Treatment of filaments, films, and similar materials containing organic derivatives of cellulose
US2058427A (en) Textile material
US2553483A (en) Production of cellulose ester yarns suitable for conversion into staple fiber
US2487833A (en) Process of saponifying yarn cakes
US2447567A (en) Stretching of cellulose ester yarn
US2072251A (en) Manufacture or treatment of artificial materials
US1920188A (en) Production of artificial materials
US2478331A (en) Production of high tenacity cellulose derivative yarns
US2083694A (en) Manufacture of artificial materials
US2088589A (en) Manufacture or treatment of materials made of or containing cellulose esters or ethers
US2112236A (en) Manufacture of artificial filaments
US2121040A (en) Production of textile materials