U.S. patent number 3,583,140 [Application Number 04/849,365] was granted by the patent office on 1971-06-08 for yarn bulking apparatus.
This patent grant is currently assigned to Badische Anilin-& Soda-Fabrik Aktiengesellschaft. Invention is credited to Walter Laber, Friedrich Lorenz.
United States Patent |
3,583,140 |
Lorenz , et al. |
June 8, 1971 |
YARN BULKING APPARATUS
Abstract
Apparatus for manufacturing bulky yarns employing flowing
gaseous or liquid media by the false twist technique. It consists
of a tubular yarn guide chamber and a lateral conduit for the fluid
medium disposed perpendicularly to the axis of the guide chamber
and opening into same tangentially to the internal wall thereof,
the guide chamber being cylindrical and at the yarn inlet end
having a drastically reduced cross-sectional area compared to the
cross section of the remainder of the chamber. The fluid inlet is
located immediately downstream of the yarn inlet end (in the
direction of movement of the yarn) in the enlarged portion of the
chamber. The latter narrows at a point downstream of the fluid
inlet (in the direction of movement of the yarn) and subsequently
opens into a tubular duct the internal wall of which contains
groovelike recesses over at least part of its length.
Inventors: |
Lorenz; Friedrich (Neustadt,
DT), Laber; Walter (Gimmeldingen, DT) |
Assignee: |
Badische Anilin-& Soda-Fabrik
Aktiengesellschaft (Ludwigshafen Rhine, Land Rhineland-Pfalz,
DT)
|
Family
ID: |
5706022 |
Appl.
No.: |
04/849,365 |
Filed: |
August 12, 1969 |
Foreign Application Priority Data
|
|
|
|
|
Aug 16, 1968 [DT] |
|
|
1,785,140 |
|
Current U.S.
Class: |
57/289; 57/333;
28/272 |
Current CPC
Class: |
D02G
1/04 (20130101) |
Current International
Class: |
D02G
1/04 (20060101); D02g 001/02 (); D02g 001/16 () |
Field of
Search: |
;57/34,34B,77.3,157F
;28/1.3,1.4,72.11,72.12 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Gilreath; Stanley N.
Assistant Examiner: Schroeder; Werner H.
Claims
We claim:
1. Apparatus for the manufacture of bulky yarns using a fluid
medium by the false twist technique, said apparatus comprising of a
tubular yarn guide chamber and an inlet for the fluid medium, said
inlet being disposed perpendicularly to the axis of the guide
chamber and opening into same tangentially to the internal wall
thereof, the guide chamber being cylindrical and having a yarn
inlet end of drastically reduced cross section compared with the
cross section of the remainder of the chamber, and the fluid inlet
being located immediately downstream of the yarn inlet end (in the
direction of movement of the yarn) in the chamber, wherein the yarn
guide chamber, at a constriction narrows downstream of the fluid
inlet (in the direction of yarn movement), and thereby opens into a
tubular duct, of reduced cross section the internal wall of which
contains groovelike recesses over at least part of its length.
2. Apparatus as claimed in claim 1, in which the groovelike
recesses are disposed parallel to the axis of the tubular duct.
3. Apparatus as claimed in claim 1, in which the groovelike
recesses are disposed perpendicularly to the axis of the tubular
duct.
4. Apparatus as claimed in claim 1, in which the groovelike
recesses extend helically around the duct axis.
5. Apparatus as claimed in any preceding claim, in which the
constriction of the yarn guide chamber is conical.
Description
The present invention relates to apparatus for the manufacture of
bulky yarns, i.e. yarns made up of random-convoluted individual
filaments, using a fluid medium by the false twist technique, said
apparatus consisting of a tubular yarn guide chamber and an inlet
for the fluid medium said inlet being disposed perpendicularly to
the axis of the guide chamber and opening into the same
tangentially to the internal wall thereof, the guide chamber being
cylindrical and having a drastically reduced cross-sectional area
at the yarn inlet end compared with the cross section of the
remainder of the chamber, and the fluid inlet being located
immediately downstream of the yarn inlet end (in the direction of
movement of the yarn) in the enlarged portion of the chamber.
Apparatus of this kind are already known in which the yarn guide
chamber is a smooth-walled tube of uniform cross section. The yarn
to be treated is supplied to the yarn inlet by means of feed rolls,
picked up by the tangentially entering fluid in the enlarged
section following the yarn inlet and given a rotational movement,
and subsequently withdrawn from the guide chamber by means of
takeup rolls. In this treatment, the yarn is twisted, heat-set by
the fluid and subsequently backtwisted.
The disadvantage of this apparatus, however, is that the yarn
produced by it is not sufficiently bulked and the desired wool
character is not quite satisfactory.
It is an object of the present invention to provide an apparatus
for making bulked yarn which, compared with yarn treated with
conventional equipment, has an improved bulkiness.
This object is achieved in accordance with the invention in an
apparatus comprising a tubular yarn guide chamber and a lateral
conduit for the fluid medium disposed perpendicularly to the axis
of the guide chamber and opening into the same tangentially to the
internal wall thereof, the guide chamber being cylindrical and
having a drastically reduced cross-sectional area at the yarn inlet
end compared with the cross section of the remainder of the
chamber, the fluid inlet being located immediately downstream of
the yarn inlet end (in the direction of movement of the yarn) in
the enlarged portion of the chamber, wherein said yarn guide
chamber narrows downstream of the fluid inlet (in the direction of
yarn movement), and subsequently opens into a tubular duct the
internal wall of which contains groovelike recesses over at least
part of its length. The groovelike recesses may run parallel or
perpendicular to the axis of the tubular duct or run on helical
paths around the duct axis. The constriction of the chamber will
preferably have a conical shape.
Two embodiments of apparatus in accordance with the invention are
illustrated diagrammatically in the accompanying drawings and will
be described in greater detail hereinafter:
FIG. 1 is a longitudinal section through one of the embodiments of
apparatus in accordance with the invention;
FIG. 2 illustrates the front elevation of the apparatus shown in
FIG. 1;
FIG. 3 is a longitudinal section through another embodiment of
apparatus in accordance with the invention;
FIG. 4 illustrates the overall arrangement of the apparatus in side
elevation;
FIG. 5 is an untreated bundle of filaments supplied to an apparatus
in accordance with the invention and viewed in side elevation
(magnification about 10 times); and
FIG. 6 is a bundle of bulked filaments seen after leaving the
bulking device (magnification about 10 times).
The apparatus in accordance with the invention, used to produce
bulked yarns, consists in accordance with FIGS. 1 to 3 of a yarn
guide chamber 1 with a lateral conduit 3 for the fluid medium which
opens tangentially to the internal wall, an inlet opening 2 for the
yarn to be treated, said opening being coaxial to chamber 1, and a
tubular duct 4 which, in the direction of movement of the yarn,
adjoins the conically narrowed portion 6 of chamber 1. The tubular
duct 4 is provided on its internal wall with groovelike recesses 5,
7 which may for example be located parallel to the duct axis (FIG.
1) or perpendicular thereto (FIG. 2).
The yarn to be treated which is in the form of a bundle of
filaments, is supplied in the manner shown in FIGS. 1 to 4 by feed
rolls 8 and 9 through inlet opening 2 into chamber 1. In chamber 1,
the yarn is picked up by the tangentially injected fluid 3, given a
rotational movement and carried onward in the direction of duct 4.
The cross section of inlet 2 is so small in relation to the cross
section of chamber 1 and duct 4, that only a very small quantity of
the fluid injected through conduit 3 can escape through inlet 2 and
the main direction of flow of said fluid is toward duct 4. Through
the superimposition of the rotational and axial movements of the
yarn within the yarn guide chamber the yarn is twisted and
backtwisted. On its passage through duct 4 connected to chamber 1,
the yarn, because of the secondary eddies produced in the fluid
medium in the groovelike recesses 5, 7, and at the edges thereof,
is additionally convoluted and made bulky. This bulking process is
assisted by the turbulence produced by the fluid in duct 4 causing
the fiber bundle to oscillate. The treated yarn is supplied to a
wind-up device via takeup rolls 11 and 12 or direct to a further
processing stage.
The fluid medium can be a gas or a liquid which is supplied to the
treatment chamber by a blower or a pump as the case may be. Air or
steam is preferred. In order to produce a permanently bulked yarn,
the latter, if consisting of threads of a thermoplastic synthetic
material, should be plastically deformable during treatment. This
can, for example, be achieved by using a gas as the fluid medium
which has been heated prior to entry into the treatment chamber to
a temperature at which the threads are plastically deformed, or the
treatment chamber itself is directly heated or alternatively a
fluid medium is used which softens the threads by chemical action.
It is equally conceivable that an apparatus in accordance with the
invention for producing bulked yarns could directly follow a
spinneret so that the yarn could be fed into the treatment chamber
while still in a plastic condition.
The advantage of a device in accordance with the invention, as
compared with known bulking apparatus, resides essentially in the
fact that yarn treated in a device according to the invention shows
superior bulk and contains no loops, coils or whorls which, during
further processing, could snag in the yarn-guide devices and thus
create problems. An apparatus in accordance with the invention is
furthermore very simple in design and its dimensions, in particular
the diameters of the individual chambers and inlets and outlets, as
well as the length and depth of the groovelike recesses, can be
adapted to any operating conditions and to the desired degree of
bulking.
EXAMPLE
In order to bulk an 18 denier 67-filament thermoplastic polyamide
yarn (see FIG. 5) an apparatus was used of the kind shown in FIGS.
1 and 2. The fluid medium used was air and this was heated to about
140.degree. C. prior to entry into the apparatus. The initial yarn
illustrated in FIG. 5 was supplied to the device at the rate of
about 250 m/min. The bulked yarn coming from the device has the
appearance shown in FIG. 6, and contained no coils or loops.
The temperature to which the yarn must be heated during the
treatment depends upon the material and can vary within wide
limits. It has been found that good results are achieved if the
yarn used in this example is heated prior to or during the
treatment to a temperature of between around 80.degree. and
170.degree. C. With crystalline thermoplastic material it must of
course be borne in mind that the crystallite melting temperature
should not be exceeded. The temperature of the air used for fluid
medium is dependent upon the time of dwell of the yarn in the air
environment, and can exceed the indicated temperature maxima.
* * * * *