U.S. patent number 3,889,325 [Application Number 05/326,559] was granted by the patent office on 1975-06-17 for process for shrinking non-woven webs.
This patent grant is currently assigned to VEPA AG. Invention is credited to Heinz Fleissner.
United States Patent |
3,889,325 |
Fleissner |
* June 17, 1975 |
Process for shrinking non-woven webs
Abstract
A process for the production of felts by shrinking a continuous
random web of textile material which includes the steps of heating
the material to be treated shock-like to a shrinking and
heat-setting temperature and drawing a heated treatment medium
through the web of material while it is being conveyed on a
perforated surface of at least one sieve drum means, the
differential pressure across the web of material on said surface
being less than the shrinkage forces whereby a uniform shrinkage of
the material is obtained.
Inventors: |
Fleissner; Heinz (Egelsbach
near Frankfurt am Main, DT) |
Assignee: |
VEPA AG (CH)
|
[*] Notice: |
The portion of the term of this patent
subsequent to March 31, 1987 has been disclaimed. |
Family
ID: |
27181422 |
Appl.
No.: |
05/326,559 |
Filed: |
January 24, 1973 |
Related U.S. Patent Documents
|
|
|
|
|
|
|
Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
|
850549 |
Aug 5, 1969 |
|
|
|
|
Foreign Application Priority Data
|
|
|
|
|
Aug 17, 1968 [DT] |
|
|
1785165 |
|
Current U.S.
Class: |
26/18.5; 68/903;
34/115 |
Current CPC
Class: |
D06C
29/00 (20130101); D04H 1/06 (20130101); D06C
7/02 (20130101); Y10S 68/903 (20130101) |
Current International
Class: |
D06C
7/00 (20060101); D06C 29/00 (20060101); D06C
7/02 (20060101); D04H 1/00 (20060101); D04H
1/06 (20060101); D06c 001/08 (); D06c 027/00 () |
Field of
Search: |
;26/18.5
;28/72HR,72NW,72.17 ;34/115 ;68/DIG.5 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
942,930 |
|
Nov 1963 |
|
GB |
|
1,004,909 |
|
Sep 1965 |
|
GB |
|
Primary Examiner: Mackey; Robert R.
Attorney, Agent or Firm: Craig & Antonelli
Parent Case Text
CROSS REFERENCE TO RELATED APPLICATION
This application is a continuation of application Ser. No. 850,549,
filed Aug. 15, 1969, now abandoned.
Claims
What is claimed is:
1. A continuous process for the production of felts by shrinking a
continuous random web of textile material which comprises
overfeeding a web of textile material to a perforated surface of at
least one sieve drum means subjected to a suction draft, conveying
said web of textile material on said perforated surface, said web
being retained on said perforated surface only by said suction
draft, heating the textile material to a shrinking temperature by
drawing a heated treatment medium through the web of material while
the web is being conveyed on the perforated surface, the
differential pressure across the web of material on said perforated
surface being lower than about 40 mm. water column which is less
than the shrinkage forces acting on said web of textile material
whereby a uniform shrinkage of the web of material is obtained on
said perforated surface, and further heating the web of shrunk
textile material on a perforated surface of at least one other
sieve drum means subjected to a suction draft to effect
heat-setting of said textile material while said web is in a
smoothed-out condition.
2. The process of claim 1, wherein the differential pressure at the
web of material is lower than about 20mm water column.
3. The process of claim 1, comprising overfeeding the web of
material to the surface of the first sieve drum longitudinally and
laterally such that the width and the length of said web of
material is conveyed on said sieve drum in a corrugated state.
4. The process of claim 1, wherein the continuous random web
comprises at least one synthetic fiber type selected from the group
consisting of polyvinyl chloride, polyvinyl alcohol and
polyacrylonitrile.
5. The process of claim 1, wherein steam is blown against both
sides of the web of material before the material is placed on the
perforated surface of the sieve drum means through which said
treatment medium is drawn to effect shrinkage of said material.
6. The process of claim 1, wherein the textile material consists of
at least two different types of fibers, one fiber type shrinking
substantially more under the influence of heat than the other.
7. The process of claim 1, wherein the web of textile material is
first penetrated by a treatment liquid with a temperature greater
than about 90.degree.C. to effect shrinkage of said material on
said perforated surface of said at least one sieve drum means and
thereafter the web of material is heated by a gaseous treatment
medium to a higher temperature for drying and refixing of said
material on the perforated surface of said at least one other sieve
drum means.
8. The process of claim 7, wherein the gaseous treatment medium is
heated to a temperature ranging from 140.degree. to
220.degree.C.
9. The process of claim 7, wherein the web of material is sprayed
with cold water before it is penetrated by the treatment
liquid.
10. The process of claim 7, wherein the continuous random web
comprises at least two different fiber types selected from the
group consisting of polypropylene and a polyamide, polypropylene
and a rayon staple, polypropylene and a polyester, polyamide
high-shrink fibers and normal polyamide fibers, polyester
high-shrink fibers and normal polyester fibers.
Description
BACKGROUND OF THE INVENTION
The present invention relates to a process for the production of
felts, particularly synthetic leather, by shrinking a continusous
random web which contains at least two fiber types. Typical
combinations of fiber types include for example, polypropylene and
a polyamide, polypropylene and rayon staple, polypropylene and a
polyester, polyamide high-shrink fibers and normal polyamide
fibers, polyester high-shrink fibers and normal polyester fibers,
combinations of other synthetic fibers and the like. According to
the present process, one fiber of said combination of fibers
shrinks substantially more under the influence of heat than the
other one of said combination of fibers. Advantageously, the
continuous random web is needled before shrinking.
It is well known to produce felts by shrinking wherein a certain
portion high-shrink fibers are added to the felts. Shrinking is
effected either in a water bowl or by jetting the web with hot air
or, in the case of a polyamide, by treating said polyamide with
steam. The well known processes exhibit the disadvantages that the
felts are corrugated after the shrinking process and accordingly
optimum shrinkage values are not obtained.
SUMMARY OF THE INVENTION
An object of the present invention is to avoid the prior art
disadvantages in processes for the production of felts.
Another object of the present invention is to provide an improved
process for the production of felts wherein the production of
denser and smoother felts is effected by means of shrinking.
Other objects and further scope of applicability of the present
invention will become apparent from the detailed description given
hereinafter.
It should be understood, however, that the detailed description and
specific examples, while indicating preferred embodiments of the
invention, are given by way of illustration only, since various
changes and modifications within the spirit and scope of the
invention will become apparent to those skilled in the art from
this detailed description.
Pursuant to the present invention, it has been found that the
abovementioned disadvantages may be eliminated and a much improved
process for the production of felts may be obtained by heating a
continuous random web shock-like or rapidly to he shrinking and/or
heat-setting temperature and by drawing a gaseous and/or vaporous
or liquid treatment medium around and through the web of material,
at least during a portion of the shrinking and/or heat-setting
treatment stage, while it rests on a plane or a curved permeable
support, such as for example, a sieve drum means.
The conveying element may be a sieve subjected to a suction draft,
advantageously one or more sieve drum means. As a result of the
suction draft the web or the felt is forced onto the sieve drum,
and thus a completely smooth felt is produced. Up to now, it was
considered impossible to use conveying elements subjected to a
suction draft for shrinking purposes in felt production because it
was feared that the suction draft would hold the web too firmly to
the sieve and also that shrinkage would not be uniform over the
entire working width, that is, it was expected that the material
would shrink more at the edge portions than in the middle portions
of the material length. With the common treatment devices with
sieve drums subjected to a suction draft, this effect actually does
occur. Here the suction draft is stronger than the shrinkage
forces. However, in accordance with the present invention, it has
been found that a uniform shrinkage can be obtained using conveying
elements subjected to a suction draft, for example, sieve drum
means, if the differential pressure used in producing the suction
draft at the web is lower than about 40mm water column, preferably
lower than about 20mm water column. A particularly dense felt, as
is required for synthetic leather is obtained if the material being
treated is first penetrated by a treatment liquid at a temperature
in excess of about 90.degree.C and subsequently by a gaseous or
vaporous treatment medium, for example, air with a temperature of,
for example, in excess of about 140.degree.C, for drying and
refixation. By said refixation, it is made sure that the other
fiber component also shrinks. In case of polyester fibers, the
refixation temperature should be about 220.degree.C, whereas in the
case polypropylene fibers a temperature of about 140.degree.C is
sufficient for said refixation.
In order to achieve a shock-like shrinkage, if shrinkage is
effected by means of a liquid, it is suggested to spray a cold
treatment liquor, for example, water, onto the web before the
shrinking treatment. In this way, a certain pre-shrinkage by the
steam rising from the treatment bowl is avoided. Such a
pre-shrinkage is very detremental because the optimum shrinkage
values cannot be reached with high-shrink fibers. It is well known
that high-shrink fibers shrink an an amount up to about 50%.
Particularly with very wide material lengths of about 1.5m and
more, it is advantageous if the web is exposed to the influence of
the treatment medium before it is supported on the sieve means.
Here it is particularly desirable if the web is overfed in a
wave-like manner before it is deposited on the sieve means
subjected to a suction draft, that is, generally a sieve drum means
subjected to a suction draft. An overfeeding of the material in the
lengthwise direction according to the desired shrinkage values
must, of course, be insured. Such an overfeed in width and an
overfeed of the material in length can, for example, be achieved by
means of a pair of rollers which are provided with annular grooves
and rings which are arranged in such a way that a ring of one
roller is situated above a recess of the other roller. By the
displacement of the one roller against the other roller, the
individual rings engage, more or less, with the recesses, that is,
with the annular grooves of the other roller and the needled web is
thus passed into the treatment medium atmosphere and/or passed to
the conveying element subjected to a suction draft in a more or
less corrugated condition. The other surface of the rings should be
bulged and/or have the shape of a torus in order to avoid marking
the edge of the material.
After the webs are fully shrunk they are generally impregnated with
bonding agents, for example, with synthetic latex, in order to
obtain a leather-like structure. Another possibility of bonding the
felt according to the present invention is to add melt fibers to
the continuous random web of material and to effect bonding
simultaneously with the shrinking and/or heat-setting treatment. If
the felts are to be used for the production of synthetic leather,
the bonded felts can be subsequently impregnated with a latex, if
necessary. However, in many cases such a latex impregnation is no
longer necessary. The felts can be subsequently coated or further
processed in the usual way.
As an apparatus for carrying out the process according to the
present invention, a device is suggested which comprises at least
one sieve means subjected to a suction draft, for example, at least
one sieve drum means subjected to a suction draft, which is
provided with an inlet unit which permits the feeding and/or
passage of the web of material with a variable overfeed (wave-like)
in length and/or in width. Furthermore, a variable speed drive for
establishing variations in the pump and/or fan speeds, is to be
correlated to the pump and/or the fan for the production of the
suction draft.
It has been found that it is of particular advantage for treating
thin webs of material to use a sieve roller subjected to a
preferably strong suction draft as an inlet unit, since such a
roller ensures an absolutely uniform overfeed of the material over
the entire working width.
It is advantageous if the sieve drum heat-setting means is combined
with a sieve drum bowl in which the web is freely guided in the
treatment liquor over a distance of at least 5cm, preferably about
10cm or more, before it is deposited on the sieve drum. Also, it is
desirable to pass the web, with an overfeed in width (wave-like)
into the treatment liquor.
Instead of the synthetic fibers which have been mentioned above,
any other suitable synthetic fibers can, of course, be used for
producing the felts of the present invention. Suitable fibers
include, for example, polyvinyl chloride, polyvinyl alcohol,
polyacrylonitrile, and the like.
BRIEF DESCRIPTION OF THE DRAWINGS
The present invention will become more fully understood from the
detailed description given hereinbelow and the accompanying
drawings which are given by way of illustration and thus are not
limitative of the present invention and wherein,
FIG. 1 is a longitudinal suction of a sieve drum apparatus
according the present invention;
FIG. 2 is a longitudinal section of another sieve drum apparatus
according to the present invention;
FIG. 3 is a longitudinal section of a combination of a sieve drum
bowl with a sieve drum heat-setting means;
FIG. 4 is a longitudinal section of still another sieve drum
apparatus according to the present invention;
FIG. 5 is a cross sectional view of the aforementioned sieve drum
apparatus, and;
FIG. 6 shows a pleating roller having rings to effect lateral
overfeeding of the textile material.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring now to the drawings, wherein like reference numerals are
used throughout the various views to designate like parts, the
apparatus of the present invention comprises a heat-insulated
housing 1 which is subdivided by a partitions means 2 into a
treatment chamber 3 and a fan chamber 4. In the treatment chamber 3
sieve drums 5 for guiding the material are disposed as well as
sieve sheets 6 which are provided above and beneath the sieve drums
5. The sieve sheets serve for equalizing the treatment medium flow.
A fan 7 is correlated to at least one face of each sieve drum 5.
This fan 7 draws the treatment medium out of the sieve drums and
recirculates it back into the treatment chamber 3 via heater
batteries 8 so that a constant circulation of the treatment medium
is ensured. If the treatment medium is air, some fresh air is
generally drawn into the device at the discharge end of the
apparatus. An equal amount of the stale, moisture enriched air is
discharged above the inlet of the apparatus.
In the apparatus according to FIGS. 1 and 2, a web 9 to be shrunk
is fed to the first sieve drum 5 by means of conveyor belt 10 and
roller 11. In the apparatus according to FIG. 1 the treatment
medium is blown out of the first sieve drum. In this way an
unrestricted shrinkage of the web 9 is ensured. With the second
sieve drum 5 the treatment medium flows from the outside to the
inside of the sieve drum and thus the web 9 is held to said sieve
drum. At the same time, an ironing effect is obtained by the
suction draft. At the outlet of the apparatus according to FIG. 1 a
conveyor belt 10 is again arranged. The device according to FIG. 2
is provided with a roller 12 at the discharge end of the
apparatus.
In the apparatus according to FIG. 2 the first sieve drum 5 is also
subjected to a suction draft. Here, material shrinkage can be
obtained in an effective way by having the conveyor belt 10 and the
roller 11 rotate at a higher speed than the sieve drum 5, so that
the web is fed wave-like to the sieve drum and allowed to shrink
freely. By the utilization of a pair of rollers provided with rings
and annular grooves which are staggered with respect to each other,
it is possible to obtain a corresponding overfeed in the width.
In each sieve drum a stationary baffle 13 is provided at that side
of the sieve drum which is not covered with the material being
treated, said stationary baffle means interrupting the suction
draft and/or the blowing effect at that side of the sieve drum
means.
The apparatus according to FIG. 3 is of similar design as that of
FIG. 2 with the exception that at the inlet of the heat-setting
chamber a pair of rollers 14 are arranged whereas at the outlet of
said chamber a chute 15 is arranged. To the heat-setting apparatus
a bowl 16 with a sieve drum 17 subjected to a suction draft is
correlated and a spray means 25 is provided for spraying water onto
the web 9 before the shrinkage treatment. Also, in this case it is
possible to overfeed the needled web 9 to the sieve drum 17 by
means of a pair of rollers 18. Subsequently, the web 9 which has
been shrunk in the bowl is squeezed by means of a squeezer 19 and
is dried and refixed on a subsequent sieve drum heat-setting
means.
The apparatus according to FIG. 4 is of similar design as that
according to FIG. 2 with the exception that the needled web 9 is
passed to the first sieve drum 5 through a vertical duct 20. In
this duct steam is sprayed onto both sides of the material by means
of jet tubes 21. Also, here it is advantageous if the pair of inlet
rollers 14' is provided with rings and/or annular grooves in order
to achieve a wave-like feeding of the materials and thus a more
uniform shrinkage (as shown in FIG. 6).
As may be gathered from FIG. 5, a drum drive 22 is arranged at one
side of the housing and a fan drive 23 with a variable speed gear
24 is provided at the other side of the housing.
The invention being thus described, it will be obvious that the
same may be varied in many way. Such variations are not to be
regarded as a departure from the spirit and scope of the invention,
and all such modifications as will be apparent to one skilled in
the art are intended to be included.
* * * * *