US808148A - Process of forming filaments from viscose, &c. - Google Patents

Process of forming filaments from viscose, &c. Download PDF

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Publication number
US808148A
US808148A US26589305A US1905265893A US808148A US 808148 A US808148 A US 808148A US 26589305 A US26589305 A US 26589305A US 1905265893 A US1905265893 A US 1905265893A US 808148 A US808148 A US 808148A
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tension
thread
bath
threads
viscose
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US26589305A
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Charles A Ernst
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SILAS W PETTIT
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SILAS W PETTIT
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Priority to US26589305A priority Critical patent/US808148A/en
Priority to US272844A priority patent/US808149A/en
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    • 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

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  • My invention relates to the manufacture of what is commonly known as artificial silk and filaments from viscose and like material, and has for its object the giving to the threads or filaments greater strength and luster, and generally the production of a superior article of manufacture.
  • Figure 1 represents a longitudinal section of apparatus.
  • Fig. 2 is a cross-section taken on the line 2 2 of Fig. l.
  • Fig. 3 illustrates a modied form in section.
  • Fig. 4 is a detailed View of construction for adjustably supporting the bars or rods l and 5 with respect to each other upon the tank of the setting-bath.
  • the tank of the setting-bath is indicated by l, which is kept lled with ammonium sulfate and bisuliite of soda or similar solution.
  • FIG. 3 represents a perforated head with either round or elongated perforations secured to the tube 2, through which the cellulose is ejected into the setting-bath within the tank l either in the form of a round thread or a series of round threads or in the form of a flat thread or tape or a series of the same.
  • Sufiicient material is forced or ejected through the cap or head into the setting-bath to allow the ends to be secured to one of the series of spools 7 after4 passing between the rods or bars A and 5, as shown in the drawings.
  • the spool 7 is then given a rotary motion in the direction of the arrow, which draws the filaments through the setting-bath at a desired predetermined tension.
  • the greatest tension upon the filamentous material may be exerted upon that portion of the threads which extends between the spool 'T and the rod 5, which portion having passed through the setting-bath is more solid and substantially evenly so throughout that portion of its length. Less tension is upon that portion of the threads or filaments which extends between the rods 1f and 5, and the least tension is upon the more plastic portion which extends between the rod et and the cap of the perforated head 3. The weakest and.
  • the tank l is filled with suitable solution, such as ammonium sulfate and bisulfite of soda and such as is commonly used in manufacturing filaments of this character from viscose and like material.
  • suitable solution such as ammonium sulfate and bisulfite of soda and such as is commonly used in manufacturing filaments of this character from viscose and like material.
  • the filaments of viscose are rendered insoluble and substantially solid after passing' through the bath.
  • the amount of friction pn the rods l and 5 and the tension on the threads may be varied by changing the relative position of the rods. As shown in Fig. 3, the rods may be so placed that the strands wrap around a considerable portion of the pe riphery of each rod. Such an arrangementis desirable where it is preferred to put a considerable amount of stretch into the thread.
  • the upper rod 5 is mounted at one end of the movable support 9, while the other rod l is mounted in the fixed support 6.
  • the support 9 is adjustable by means of the slot l() and thumb-screw il. By this means the rods a and can be readily and accurately adjusted relatively to each other to produce the proper tension 'for any character of thread.
  • the threads or filaments may be spun together in the setting'- bath or not, as desired.
  • a flat, as well as a round, thread or a series of the same may be formed, as desired.

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

Description

No. 808,148. PATBNTED DEG. 26, 1905.
c. A. ERNST.
PROCESS 0F PORMING FILAMBNTS PROM VISGOSE, Se,
' APPLICATION FILED JUNE 19.1905.
S2 y lhlnwll v 1H`1ll1i|||li i Il M :.911 l Il( VEN TUI? QM A 5r 42;@ WM5 TTUHNEY. l
` WITHESSES.:
UNITED STATES PATENT OEEICEo CHARLES A. ERNST, OF LANSDOVNE, PENNSYLVANIA, ASSIGNOR TO SILAS IV. PETTIT, OF PHILADELPHIA, PENNSYLVANIA.
Specification of Letters Patent.
Patented Dec. 26, 1905.
Application iiled June 19,1905. Serial No. 265,893.
To rr/ZZ whom it mar/,U concern:
Be it known that l, CHARLES A. ERNST, a citizen of the United States, and a resident of Lansdowne, State of Pennsylvania, have invented certain new and useful Improvements Relative to the Process of Forming Filaments from Viscose, &c., of which the following is a full, clear, and exact description, reference being had to the accompanying drawings, forming a part of this specification.
My invention relates to the manufacture of what is commonly known as artificial silk and filaments from viscose and like material, and has for its object the giving to the threads or filaments greater strength and luster, and generally the production of a superior article of manufacture.
In the manufacture of threads and filaments from viscose it is advantageous to spin the thread directly onto spools and to treat the thread in all the further stages of reverting, washing, and drying while it remains on the spool. In order to obtain a luster to the thread or filament, such as made from viscose, it is necessary to dry them while under tension. The degree of tension is also a very important element in the drawing stage of the process, and my present invention relates mainly to the method of subjecting the threads in the drawing stage of the process at a certain portion in their length between the spool and the perforated cap to an unevenly-distributed tension while the threads are still in a semiplastic condition, thereby imparting greater and more uniform strength and adding greater luster. In the methods heretofore practiced in the manufacture of threads of this character from viscose and like material the tension upon the threads has been produced by drawing the filaments through the setting-bath directly from the perforated cap; but this tension is incidental and insufficient to produce the best results. In the methods heretofore practiced it has been impossible to exert upon the filaments the desired amount of tension, as the greatest strain is upon that portion of the thread where it is the most plastic, which is of course the point where the plastic material rst enters the setting-bath from the perforated cap, or the point where the threads first enter the setting-bath. Therefore a limited amount of tension only can be exerted. This is suficient to produce practical results for some sizes, but not the best results, as I A have discovered in my practical experience.
In carrying out myinvention for giving additional strength and luster to the threads I subject the threads in a portion intermediate in their length between the spool and the cap or perforated head to an increased tension after this portion has become partially solidified substantially evenly in this portion of its length by passing through the setting-bath.
My invention consists in the method hereinafter more particularly described, and specified in the claims.
The operation of my process and two forms of apparatus for carrying the same out are illustrated in the drawings forming part of this specification.
Figure 1 represents a longitudinal section of apparatus. Fig. 2 is a cross-section taken on the line 2 2 of Fig. l. Fig. 3 illustrates a modied form in section. Fig. 4 is a detailed View of construction for adjustably supporting the bars or rods l and 5 with respect to each other upon the tank of the setting-bath.
The tank of the setting-bath is indicated by l, which is kept lled with ammonium sulfate and bisuliite of soda or similar solution.
2 represents one of a series of tubes through which the viscose or like solution is forced under pressure, as is usual in an apparatus of this character, the details of which are not shown.
3 represents a perforated head with either round or elongated perforations secured to the tube 2, through which the cellulose is ejected into the setting-bath within the tank l either in the form of a round thread or a series of round threads or in the form of a flat thread or tape or a series of the same. Sufiicient material is forced or ejected through the cap or head into the setting-bath to allow the ends to be secured to one of the series of spools 7 after4 passing between the rods or bars A and 5, as shown in the drawings. The spool 7 is then given a rotary motion in the direction of the arrow, which draws the filaments through the setting-bath at a desired predetermined tension. By the interposition of the rods t and 5, arranged as indicated in Figs. l and 3 or in a substantially like manner and crosswise of the tank, the greatest tension upon the filamentous material may be exerted upon that portion of the threads which extends between the spool 'T and the rod 5, which portion having passed through the setting-bath is more solid and substantially evenly so throughout that portion of its length. Less tension is upon that portion of the threads or filaments which extends between the rods 1f and 5, and the least tension is upon the more plastic portion which extends between the rod et and the cap of the perforated head 3. The weakest and. most ductile portion, it will be observed, is of course that portion of the threads as it emerges in the semiplastic condition from the perforated cap and before it has been in the setting-bath any length of time. If the same tension should be exerted upon this portion of the threads as may be exerted upon the portion between the spool 7 and the rod 5, it would either break off the threads or draw them entirely too finely and either weaken or destroy the thread or filament. After the thread has passed the rod 5 on its passage to the spool 7 while it is substantially still very ductile the amount of tension which is capable of be ing exerted upon the thread at this stage without drawing the thread or filament is much greater than that which may be exerted at the primary stage, and therefore the threads or filaments at this portion may be subjected to a much greater tension, adding greater luster to the thread as well as imparting to it greater strength.
While the drawings only represent one set of tubes and perforated caps and threads or filaments and spools, a series are preferably arranged of similar character side by side at proper intervals apart throughout the width of the tank, as indicated in Fig. 2.
8 represents a vibrating thread-guide by means of which the strands are laid in layers or courses upon each spool.
The tank l is filled with suitable solution, such as ammonium sulfate and bisulfite of soda and such as is commonly used in manufacturing filaments of this character from viscose and like material. By the action of this solution the filaments of viscose are rendered insoluble and substantially solid after passing' through the bath. The amount of friction pn the rods l and 5 and the tension on the threads may be varied by changing the relative position of the rods. As shown in Fig. 3, the rods may be so placed that the strands wrap around a considerable portion of the pe riphery of each rod. Such an arrangementis desirable where it is preferred to put a considerable amount of stretch into the thread.
In the form shown in Fig. l the rods are submerged. It is clear that one or both may be or neither, if desired.
In the detailed drawing shown in Fig. 4 the upper rod 5 is mounted at one end of the movable support 9, while the other rod l is mounted in the fixed support 6. The support 9 is adjustable by means of the slot l() and thumb-screw il. By this means the rods a and can be readily and accurately adjusted relatively to each other to produce the proper tension 'for any character of thread.
In my preferred form of the invention I make the rods 5 and 6 of glass; but ebonite, rubber, or other suitable material could be readily substituted.
It is clear that the construction of apparatus may be considerably varied without departing' from the spirit of my invention and that my process may be carried out by various forms of apparatus employing suitable tension devices between the spinning-head 3 and the winding-spool 7, operating in the manner hereinbefore described for carrying out my improved method.
In carrying out my process the threads or filaments may be spun together in the setting'- bath or not, as desired. A flat, as well as a round, thread or a series of the same may be formed, as desired.
Having thus described my invention, what I claim, and desire to secure by Letters Patent, is-- l. The herein-described process of making filaments from viscose, and like material, consisting in causing theviscose, or like material, to pass through a perforated cap into and through a setting-bath directly to the winding-spool, and subjecting the different portions of the length of the threads between the spool and the perforated cap to different degrees of tension to apply a definite predetermined stretch' to the filaments between the bath and the winding-spool.
2. The herein-described process of making filaments from viscose, or like material, consisting in causing the viscose, or like material, to emerge into a setting-bath in the form of a filamentous thread, passing the same through said setting-bath directly to the winding-spool, and subjecting the portion of the thread nearest the emerging-point to aminimum stretch, and the portion of the thread nearest the winding-spool to a maximum stretch.
3. The process of making filaments from viscose and like material, which consists in applying' a definite predetermined stretch to the filaments as they emerge from the setting-bath and winding' the said filaments, under tension, directlyA upon spools.
4. The manufacture of threads from plastic material formed by ejecting the plastic material under pressure in the form of finely-divided filament, or thread, intoasetting-bath, winding the threads directly upon a spool under tension, and subjecting the most plastic portion of the thread in the setting-bath to a minimum stretch, and the more solidified portion nearer the winding-spool to a greater stretch.
5. The manufacture of threads from plastic material, consisting in forcing the plastic material in a finely-divided state under pressure into a setting-bath, and passing the same through the setting-bath to and upon a winding-spool, exerting friction upon the said thread at a point intermediate in its length between the spool and where the divided plastic material enters the setting-bath, and applying a greater tension upon the portion of the threads between the spool and the tension medium, and a less tension between the friction medium and the point of entry of the divided plastic material into the setting-bath.
6. The herein-described process of making filaments from viscose or like material, consisting in causing viscose or like material to emerge in a setting-bath in the form of a filamentous thread, passing the same through said setting-bath, and through a tension device to a winding-spool and subjecting the portion of the thread nearest the emergingpoint of a minimum tension, subjecting that portion of the thread passing through the tension device by a greater tension than the rst portion ofthe thread is subjected, and subjecting that portion of the thread between said tension device and the winding-spool of a maximum tension.
7. In the manufacture of laments from viscose or similar material, in which the viscose is ejected in a setting-bath and vwound directly upon spools, the process of subjecting different portions of the thread between the spinning-heads and the spools to three different tensions, whereby the minimum strain is applied to that portion of the filaments nearest the spinning-head, maximum tension is applied to that portion nearest the windingspool and a medium tension is applied to a third portion of the thread located between the portions under maximum and minimum tensions.
In witness whereof I have hereunto set my hand this 16th day of June, 1905.
CHARLES A. ERNST.
Witnesses:
CHARLES JANVIER, WALTER C. POWELL.
US26589305A 1905-06-19 1905-06-19 Process of forming filaments from viscose, &c. Expired - Lifetime US808148A (en)

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US272844A US808149A (en) 1905-06-19 1905-08-05 Apparatus for producing or forming filaments from viscose, &c.

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4332752A (en) * 1978-10-02 1982-06-01 Akzo N.V. Process for production of dialysis membrane hollow fiber chains
USD423771S (en) * 1999-02-24 2000-05-02 M.R. Carretta & Company Cosmetic bag pouch
US20070056994A1 (en) * 2005-09-12 2007-03-15 Keurig, Incorporated Drain for beverage forming machine

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4332752A (en) * 1978-10-02 1982-06-01 Akzo N.V. Process for production of dialysis membrane hollow fiber chains
USD423771S (en) * 1999-02-24 2000-05-02 M.R. Carretta & Company Cosmetic bag pouch
US20070056994A1 (en) * 2005-09-12 2007-03-15 Keurig, Incorporated Drain for beverage forming machine
US7640845B2 (en) 2005-09-12 2010-01-05 Keurig, Incorporated Drain for beverage forming machine

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