US1984472A - Manufacture of artificial threads - Google Patents

Manufacture of artificial threads Download PDF

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Publication number
US1984472A
US1984472A US361080A US36108029A US1984472A US 1984472 A US1984472 A US 1984472A US 361080 A US361080 A US 361080A US 36108029 A US36108029 A US 36108029A US 1984472 A US1984472 A US 1984472A
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United States
Prior art keywords
spinning
spinning solution
nozzle
manufacture
hollow body
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Expired - Lifetime
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US361080A
Inventor
Friederich Alfred
Schlack Paul
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Aceta G Mbh
ACETA GmbH
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ACETA GmbH
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/04Dry spinning methods
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D4/00Spinnerette packs; Cleaning thereof

Definitions

  • This invention relates to a process of and apparatus for avoiding, as far as possible, variations of the titer of the individual threads spun from the nozzle in the dry spinning of artificial threads.
  • This invention minimizes these difficulties in spinning highly viscous solutions by guiding the spinning solution which enters the spinning cell into symmetrically placed streams and in as thin layers as possible along the surface of a body of hi h heat capacity placed directly above nozzle.
  • Apparatus for realizing the invention may be constructedin various ways.
  • FIG. 1-6 of the accompanying drawing illustrate some of these ways, Figsbl, 3 and 5 being axial sections and Figs. 2,; 4 and dcorresponding cross sections.
  • the same letters of reference indicate the same-parts in all 'the figures.
  • two bodies of the highest possible heat capacity are arranged one within the other in such a manner that between them there is a space as narrow as may be for the passage of liquid, the opposite faces of the two bodies having any desired form; for example, as in the case shown, the bodies may be co-axial cylinders.
  • the outer cylinder a of a diameter of, for instance, 5 cm. having comparatively thin walls of a thickness of, for instance, 0.4 cm. is furnished for the purpose of increasing its heat capacity, with external ribs 9.
  • the massive, inner cylinder 19 is fitted into the outer cylinder and has perforations h for entering of the solution into the narrow annular space of a thickness of, for instance, 0.3-0.5 cm. between the two cylinders, these separate streams all issuing through the nozzle connected to the end of the outer cylinder.
  • the spinning solution enters through the duct e fixed in the cover 0, this latter being screwed on to the cylinder with interposition of the washer d.
  • Figs. 3 and 4 The form shown in Figs. 3 and 4 is essentially the same as that already described, but the attempt has been made to provide a larger surface of contact for heat exchange with the outer and inner cylinders.
  • the inner cylinder is provided with 16 peripheral grooves of a diameter of, for instance, 0.3-0.5 cm. in the axial direction through which the solution flows, the cylinder otherwise fitting closely in the external cylinder (1.
  • the equalizing body consists of a single piece a through which the spinning solution flows by way of 9 bores of the diameter of, for instance, 0.3-0.5 cm. parallel with the axis. Since these bores are narrow in comparison with the mass of the body, the desired homogenizing of the spinning solution is obtained more or less in the same manner as in the other construction.
  • our invention is not limited to the special forms of the homogenizing device as described. Thus, for instance, they may be arranged in combination with a special heating or cooling device in order to heat or cool them at any desired temperature.
  • a device for equalizing the temperature of the spinning solution before leaving the nozzle comprising in combination a hollow heat conducting body provided with an inlet for the spinning solution, a massive heat conducting body placed in the said hollow body, filling up the latter nearly completely and causing the spinning solution to flow in form of a thin layer between the inner face of the hollow body'andthe outer face of the massive body, and an outlet on said hollow body bearing the spinning nozzle.
  • a device for equalizing the temperature of the spinning solution before leaving the nozzle comprising in combination a cylindrical heat conducting hollow body provided with heat capacity increasing ribs and an inlet for the spinning solution, a cylindrical heat conducting massive body, placed in the said hollow body,
  • a device for equalizing the temperature of the spinning solution before leaving the nozzle comprising in combination a cylindrical heat conducting hollow body provided with an inlet for the spinning solution, a cylindrical heat conducting massive body placed in the said hollow body filling up the latter nearly completely and causing the spinning solution to flow in form of a thin layer between the inner face of the hollow body and the outer face of the massive body, means for asserting the heat exchange arranged on the outer cylinder and an outlet on said hollow body bearing the spinning nozzle.
  • a device for equalizing the temperature of a spinning solution before leaving the nozzle which comprises a body of high heat capacity, placed in the path of the spinning solution directly above the nozzle, of such a character that the spinning solution flows finely distributed over a substantial distance across said body of high heat capacity.

Description

Dec. 18, 1934. A. FRYIEDERICH ETAL MANUFACTURE OF ARTIFICIALTHREADS Filed May '7, 1929 l question of metallic bodies.
bodies of porcelain or of any artificial material may be applied. These materials even would have the advantage of higher heat capacity over This body is at the head of the spin- 45 ning shaft and is not subjected to variations of Moreover, it is possible to make its Patented Dec. 18, 1934 MANUFACTURE OF ARTIFICIALTHREADS Alfred Friederich, Berlin, and Paul Schlack, Ber-;
lin-Karlsh0rst,, Germany, assignors to Aceta Gum. b; 11., Lichtenberg, Germany, .a corporation of Germany Application May 7, 1929, Serial No. 361,080
In Germany May 15, 1928 4 Claims.
This invention relates to a process of and apparatus for avoiding, as far as possible, variations of the titer of the individual threads spun from the nozzle in the dry spinning of artificial threads.
On the way from the reservoir to the spinning nozzle the solution to be spun passes through ducts, pumps, filters and the like which are of different form, mass and surface and exposed to different temperatures, andthe passages in them is for flow of the solution are of quite dilferent It has been recognized that, particularly in the case of highly viscous solutions, these differences in cross section, in surface and therefore in transference of heat cause the solu- "5 tion to partially lose its homogeneity on its way from the reservoir to the nozzle, or at all events cross sections.
to suffer a differentiation in the viscosity of extent.
tions.
and in addition variations of the titer of individual threads, which under some conditions are increased because, in consequence of the loss of homogeneity, the portions of the solution of different viscosities have also different contents of solvent.
This invention minimizes these difficulties in spinning highly viscous solutions by guiding the spinning solution which enters the spinning cell into symmetrically placed streams and in as thin layers as possible along the surface of a body of hi h heat capacity placed directly above nozzle.
the metal.
temperature. metallic mass so large in comparison with volume of the spinning solution with which it is to be in contact that small variations in the temperature of the outside atmosphere have no effect. Thus, should the spinning solution enter this equalizing body in a partly non-homogeneous condition its gradual fiow along the body serves to homogenize it, so that it arrives at the nozzle In this manner a thorin a uniform condition.
For the desired purpose there is not only In the same manner oughly uniform spinning of the several'threads occurs without formation of sagging threads and variations of the titer of the individual threads.
Apparatus for realizing the invention may be constructedin various ways.
Figs. 1-6 of the accompanying drawing illustrate some of these ways, Figsbl, 3 and 5 being axial sections and Figs. 2,; 4 and dcorresponding cross sections. The same letters of reference indicate the same-parts in all 'the figures.
Referring to Figs. 1 and 2, two bodies of the highest possible heat capacity are arranged one within the other in such a manner that between them there is a space as narrow as may be for the passage of liquid, the opposite faces of the two bodies having any desired form; for example, as in the case shown, the bodies may be co-axial cylinders.
The outer cylinder a of a diameter of, for instance, 5 cm. having comparatively thin walls of a thickness of, for instance, 0.4 cm. is furnished for the purpose of increasing its heat capacity, with external ribs 9. The massive, inner cylinder 19 is fitted into the outer cylinder and has perforations h for entering of the solution into the narrow annular space of a thickness of, for instance, 0.3-0.5 cm. between the two cylinders, these separate streams all issuing through the nozzle connected to the end of the outer cylinder. At the other end of this cylinder the spinning solution enters through the duct e fixed in the cover 0, this latter being screwed on to the cylinder with interposition of the washer d.
The form shown in Figs. 3 and 4 is essentially the same as that already described, but the attempt has been made to provide a larger surface of contact for heat exchange with the outer and inner cylinders. For this purpose the inner cylinder is provided with 16 peripheral grooves of a diameter of, for instance, 0.3-0.5 cm. in the axial direction through which the solution flows, the cylinder otherwise fitting closely in the external cylinder (1.
In the form shown in Figs. 5 and 6, the equalizing body consists of a single piece a through which the spinning solution flows by way of 9 bores of the diameter of, for instance, 0.3-0.5 cm. parallel with the axis. Since these bores are narrow in comparison with the mass of the body, the desired homogenizing of the spinning solution is obtained more or less in the same manner as in the other construction.
As mentioned above these homogenizing devices are arranged at the head of the spinning the the
the
the
shaft and they always accept the temperature of the said spinning shaft.
It is obvious that our invention is not limited to the special forms of the homogenizing device as described. Thus, for instance, they may be arranged in combination with a special heating or cooling device in order to heat or cool them at any desired temperature.
Having now particularly described and ascertained the nature of our said invention and in what manner the same is to be performed, we declare that what we claim is:--
1. A device for equalizing the temperature of the spinning solution before leaving the nozzle comprising in combination a hollow heat conducting body provided with an inlet for the spinning solution, a massive heat conducting body placed in the said hollow body, filling up the latter nearly completely and causing the spinning solution to flow in form of a thin layer between the inner face of the hollow body'andthe outer face of the massive body, and an outlet on said hollow body bearing the spinning nozzle.
2. A device for equalizing the temperature of the spinning solution before leaving the nozzle comprising in combination a cylindrical heat conducting hollow body provided with heat capacity increasing ribs and an inlet for the spinning solution, a cylindrical heat conducting massive body, placed in the said hollow body,
filling up the latter nearly completely and causing the spinning solution to flow in form of a thin layer between the inner face of the hollow body and the outer face of the massive body, and an outlet on said hollow body bearing the spinning nozzle. v
3. A device for equalizing the temperature of the spinning solution before leaving the nozzle comprising in combination a cylindrical heat conducting hollow body provided with an inlet for the spinning solution, a cylindrical heat conducting massive body placed in the said hollow body filling up the latter nearly completely and causing the spinning solution to flow in form of a thin layer between the inner face of the hollow body and the outer face of the massive body, means for asserting the heat exchange arranged on the outer cylinder and an outlet on said hollow body bearing the spinning nozzle.
4. A device for equalizing the temperature of a spinning solution before leaving the nozzle which comprises a body of high heat capacity, placed in the path of the spinning solution directly above the nozzle, of such a character that the spinning solution flows finely distributed over a substantial distance across said body of high heat capacity.
ALFRED FRIEDERICH. PAUL SCHLACK.
US361080A 1928-05-16 1929-05-07 Manufacture of artificial threads Expired - Lifetime US1984472A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEA54182D DE496380C (en) 1928-05-16 1928-05-16 Method and device for spinning rayon threads by the dry spinning process

Publications (1)

Publication Number Publication Date
US1984472A true US1984472A (en) 1934-12-18

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US361080A Expired - Lifetime US1984472A (en) 1928-05-16 1929-05-07 Manufacture of artificial threads

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US (1) US1984472A (en)
DE (1) DE496380C (en)
FR (1) FR671637A (en)
GB (1) GB311763A (en)
NL (1) NL24695C (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2423155A (en) * 1943-11-11 1947-07-01 Philip H Phillips Pressure restricting device
US2469327A (en) * 1943-12-09 1949-05-03 Coca Cola Co Beverage dispensing device
US3353211A (en) * 1965-01-06 1967-11-21 American Enka Corp Spinneret assembly
US3360597A (en) * 1964-06-03 1967-12-26 British Nylon Spinners Ltd Melt-spinning of synthetic linear polymers
US3437725A (en) * 1967-08-29 1969-04-08 Du Pont Melt spinning apparatus and method

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE756867C (en) * 1939-08-01 1953-02-23 Ig Farbenindustrie Ag Device for regulating the temperature of electrically heated device parts
DE1169076B (en) * 1959-01-07 1964-04-30 Verreinigte Glanzstoff Fabrike Device for uniform heating of the viscose in the spinning tube
NL255435A (en) * 1959-10-14

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2423155A (en) * 1943-11-11 1947-07-01 Philip H Phillips Pressure restricting device
US2469327A (en) * 1943-12-09 1949-05-03 Coca Cola Co Beverage dispensing device
US3360597A (en) * 1964-06-03 1967-12-26 British Nylon Spinners Ltd Melt-spinning of synthetic linear polymers
US3353211A (en) * 1965-01-06 1967-11-21 American Enka Corp Spinneret assembly
US3437725A (en) * 1967-08-29 1969-04-08 Du Pont Melt spinning apparatus and method

Also Published As

Publication number Publication date
GB311763A (en) 1930-05-01
NL24695C (en)
DE496380C (en) 1930-04-23
FR671637A (en) 1929-12-16

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