U.S. patent number 3,667,422 [Application Number 04/775,819] was granted by the patent office on 1972-06-06 for apparatus for transferring a particulate material to a web.
This patent grant is currently assigned to Saladin A. G.. Invention is credited to Benno Saladin.
United States Patent |
3,667,422 |
Saladin |
June 6, 1972 |
APPARATUS FOR TRANSFERRING A PARTICULATE MATERIAL TO A WEB
Abstract
A device for adding a thermoplastic or thermosetting material to
a receiving web includes means for distributing a particulate
material throughout recesses or grooves defined on the surface of
an endless member such as a continuously rotating drum. The grooves
which have been filled with the material are then moved into
association with a web of a material such as a textile material
which is moved into contact with the drum and at the same speed as
the drum while it is maintained at a temperature great enough to
cause the tackiness and adherence of the particulate material to
the web in the pattern defined by the grooves of the drum. The
granules are advantageously directed to the top face of the drum as
it rotates and the web is advantageously delivered to a location at
which it feeds around a major portion of the lower part of the drum
surface. A pressure roller is located at the infeed of the web and
at the outfeed of the web and is advantageously maintained in a
heated condition to provide a temperature to facilitate the
transfer of the thermoplastic material from the grooves of the drum
to the surface of the web. The particulate coating material is
delivered to the backing material web at a coating station while
the material is maintained at a temperature lower than that at
which it is applied to the backing material. Conversely, the
backing material is maintained at or heated to a temperature at
which the particulate material will become tacky and move into
adhering engagement with the backing material as it is transported
into association therewith at the coating station.
Inventors: |
Saladin; Benno (Sirnach,
CH) |
Assignee: |
Saladin A. G. (Sirnach/TG,
CH)
|
Family
ID: |
3622082 |
Appl.
No.: |
04/775,819 |
Filed: |
November 14, 1968 |
Foreign Application Priority Data
|
|
|
|
|
Nov 20, 1967 [OE] |
|
|
A 10399/67 |
|
Current U.S.
Class: |
118/34; 118/202;
118/246; 118/60; 118/212; 118/641 |
Current CPC
Class: |
B05C
19/04 (20130101); D06N 3/0093 (20130101); B05D
1/28 (20130101); D21H 23/64 (20130101); B05D
2401/32 (20130101) |
Current International
Class: |
D06N
3/00 (20060101); B05C 19/04 (20060101); B05C
19/00 (20060101); D21H 23/64 (20060101); D21H
23/00 (20060101); B05D 1/28 (20060101); B05c
001/08 (); B05c 001/16 () |
Field of
Search: |
;117/13,21,25,38,111
;118/60,202,211,244,59,212,637,246,69,34,641 ;101/170,157 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: McIntosh; John P.
Claims
What is claimed is:
1. Apparatus for applying a particulate coating formed of discrete
particles which particles become tacky when heated to a certain
temperature, to a backing material, comprising a hopper for the
discrete particles in a non-tacky condition, an endless carrier
member defining a support surface for the backing material, the
support surface of said endless carrier member being patterned for
forming recesses therein arranged to receive the discrete
particles, feed means for conveying the discrete particles from
said hopper to the support surface of said endless carrier member
and for positioning the discrete particles into the recesses formed
therein and for removing any discrete particles from the remainder
of the support surface with the discrete particles being at a
temperature below the temperature at which they become tacky, means
arranged for moving and placing the backing material into contact
with the support surface of said endless carrier member including
at least one pressure member arranged in juxtaposed relationship to
the support surface of said endless carrier for contacting the
backing material against the support surface, means for driving
said endless carrier member for moving its support surface relative
to said feed means and to said pressure member, and heating means
associated with said support surface for heating the backing
material in contact with said pressure member so that it is at a
temperature at which the discrete particles become tacky when it is
placed into contact with the support surface of said endless
carrier member so that the discrete particles in the recesses in
the support surface of said endless carrier member become tacky
when contacted by the heated backing material for transferring the
discrete particles to the backing material.
2. Apparatus, as set forth in claim 1, wherein said pressure member
is a pressure roller and said means arranged to move and place the
backing material being arranged for directing the backing material
over a considerable portion of the circumferential surface of said
pressure roller.
3. Apparatus, as set forth in claim 2, wherein said means to move
and place the backing material including a second pressure roller
spaced angularly about said drum from said pressure roller and
being arranged in juxtaposed relationship to the support surface of
said drum so that the backing material contacts said drum between
said pressure roller and said second pressure roller, and said
heating means being associated with said second pressure roller for
heating the backing material.
4. Apparatus, as set forth in claim 3, wherein a heating device
being located adjacent the path of the backing material extending
from said second pressure roller for heating the particles which
adhere to the backing material.
5. Apparatus, as set forth in claim 1, wherein said endless carrier
member comprises a rotatable drum, and said means for driving said
endless carrier member comprises a shaft on which said drum is
mounted for rotation.
6. Apparatus, as set forth in claim 5, characterized in that
cooling means is associated with said drum for maintaining said
drum at a temperature at which the discrete particles do not become
tacky.
7. Apparatus, as set forth in claim 5, wherein said hopper and said
feed means being located above said drum, said feed means
comprising an oscillatable downwardly directed guide plate
positioned in the path of the discrete particles issuing from said
hopper and with its lower end closely spaced above said drum, a
shield member extending downwardly from the discharge end of said
hopper about said guide plate and having its lower end enclosing
the upper part of said drum, a doctor roller located within said
shield member and in contact with the circumferential surface of
said drum and positioned downstream from said guide member in the
rotational direction of said drum, and a doctor blade located
within said shield member and downstream from and adjacent to the
contact between said roller doctor and said drum, said blade having
its edge coinciding with the circumferential surface of said drum
for removing discrete particles from the surface without affecting
the discrete particles within the recesses in the surface.
8. Apparatus, as set forth in claim 1, wherein said means arranged
to move and place the backing material including a spherically
shaped roller arranged to stretch the backing material before it
passes over said pressure roller.
Description
SUMMARY OF THE INVENTION
This invention relates, in general, to an apparatus for coating a
backing material and, in particular, to a new and useful device for
applying a thermosetting or thermoplastic material in a defined
pattern to a web.
Various methods of applying a particulate coating to a backing
material have been proposed in the past. The expression "backing
material" as used in the present specification and claims is
intended to include sheets, strips, bands and webs of, for example,
textile and other fibrous materials such as plastics, synthetics,
resin materials, paper, cardboard, pasteboard, knitted and woven
fabrics, slubbings, wadding, fleeces and porous and non-porous
foils. The expression "particulate material" as used herein
includes materials in the form of powder, granular material, or
crystalline material, in the form of discrete particles.
It is difficult, when carrying out the previously proposed methods,
to obtain a coating of uniform thickness and even particle
distribution. Difficulties may arise as result of the properties of
the material being used to form the coating. For example, some
powders become electrostatically charged during manufacture or have
a tendency subsequent to manufacture to absorb electrostatic
charges. Repulsion between similarly charged particles complicates
the conveyance of the powder and leads to an uneven distribution of
the particles on the backing material. Furthermore, some powders
have adhesive properties which may become apparent at elevated
temperatures, and some synthetic resin powders become extremely
tacky and adhere to any firm object as a result of a very slight
rise in temperature above that at which not tackiness is
observable.
Coating methods which utilize an intermediate carrier to transfer
the coating material from a hopper to a backing material to be
coated, have proved advantageous. The intermediate carrier may be
in the form of an endless band or roller recessed to carry a
desired thickness of coating material in a desired pattern and
which passes beneath the hopper outlet and is subsequently wiped by
a doctor. Nevertheless, this method has not proved entirely
satisfactory when, for example, employed in a process for producing
a composite article comprising a moisture, water or steam pervious
backing material with a discontinuous impervious film on one or
both of its surfaces. In a process for producing such an article,
it is desired to apply a coating of powder to a surface of suitable
backing material and then compress, plasticize, sinter, vulcanize
and harden the powder coating to produce a discon-tinuous
impervious film on the pervious substrate. However, when the
particles are of a type which are, or are liable to become,
electrostatically charged, or are particularly tacky at the
operating temperature, or are extremely fine or hydroscopic, it is
difficult to ensure that the distribution of powder takes place in
such a way as to obtain the desired discontinuities.
In accordance with the invention there is provided apparatus for
applying a particulate coating to a backing material, in which the
temperature at which the material intended to form the coating is
transported to a coating station is lower than that at which the
particulate material is applied to the backing material. Preferably
the particulate material is fed from a store onto a conveying
surface which is recessed, the pattern and depth of the recesses
being in accordance with the desired distribution of the powder on
the backing material to be coated. The aforesaid lower temperature
depends for its exact value largely upon the chemical constitution
of the particulate material. If, by way of example, polyamide
powders are to be conveyed and distributed, then application onto
the conveying surface must be carried out at about 15.degree. C, so
the temperature of transportation is considerably below the
temperature at the coating station. If, on the other hand,
polyethylene powders are to be distributed, then the temperatures
of the conveying surface must be increased to 50.degree.-60.degree.
C. The higher temperatures, on the other hand, at which the
particulate material is removed from the conveying surface and
transferred onto the underlayer that is to be coated on an
intermediate carrier, can be raised to values which correspond to
the respective plastification temperature of the powder or lie only
slightly above or below it.
In the case of particles which are already electrostatically
charged, such particles may, in accordance with a preferred feature
of the invention, be passed through a Faraday cage in which the
charge is led off towards the cage surface. In order to prevent the
particles from becoming charged during the process it is possible
to utilize procedures similar to those which, for example, are
employed in the case of paper machines, to ensure that no charge is
built up during travel of the paper rolls.
The invention also provides apparatus for applying a particulate
coating to a backing material, comprising: a hopper, an arrangement
for feeding particulate material from the hopper to an endless
carrier surface, at least one pressure roller for urging the
backing material into contact with the carrier surface, and means
for maintaining the temperature of the pressure roller above that
of the carrier surface.
Accordingly, an object of the invention is to provide an improved
device for transferring a thermosetting or thermoplastic
particulate material in a defined pattern onto a web or backing
sheet.
A further object of the invention is to provide an apparatus for
transferring a particulate material first onto a grooved surface of
a rotating drum and for moving a web into association with a
portion of the surface of the drum in a manner such that the
particulate is transferred to the web, the web being maintained at
a temperature to cause the tacky adherence of the material and its
transfer out of the grooves of the drum as the drum is rotated and
the web is advanced.
A further object of the invention is to provide an apparatus for
applying a particulate material to a web in a defined pattern which
comprises distributing the particulate material over a defined
surface which is moved, and directing a backing web into
association with the defined surface while maintaining the web at a
temperature which is greater than that of the surface in order to
provide for the tacky adherence of the material to the web during
the course of travel of the web over the defined surface.
A further object of the invention is to provide an apparatus for
applying a particulate coating to a backing material which includes
the transporting of the particulate coating material from a storage
supply to a coating station and applying the material to the
backing material at the coating station, the material being
maintained during transportation at a temperature less than that at
which it is applied to the backing material.
A further object of the invention is to provide a device for
applying a thermosetting or thermoplastic material to a web in a
defined pattern which is simple in design, rugged in construction
and economical to manufacture.
The various features of novelty which characterize the invention
are pointed out with particularity in the claims annexed to and
forming a part of this specification. For a better understanding of
the invention, its operating advantages and specific objects
attained by its use, reference should be had to the accompanying
drawings and descriptive matter in which there is illustrated and
described a preferred embodiment of the invention.
BRIEF DESCRIPTION OF THE DRAWINGS
The only FIGURE of the drawings is a partial longitudinal sectional
and partial elevational view of a device for applying a coating of
material to a web constructed in accordance with the invention.
GENERAL DESCRIPTION OF THE PREFERRED EMBODIMENTS
As shown in the drawing, a hopper 1 is filled with powder to be
applied to a continuous textile web 2 in such a way that on one
surface of the web the powder is in the form of discrete spaced
particles, the thickness of the coating thus provided being
completely uniform and the distribution of the discrete particles
being even.
A rotary discharge roller 4 is located in the outlet 3 of the
hopper, and ensures that powder is taken from the hopper and passed
to a downwardly-directed guide plate 5 in an even stream. A
cam-operated vibration device 6 serves to vibrate the plate 5 so
that the powder trickles in a loose layer down the guide plate 5.
The guide plate terminates at its lower end slightly above a
distribution drum 10. The upper part of this drum, together with a
doctor roller 8, a stroking doctor 9 with a blade 14 and the lower
part of guide plate 5 and discharge roller 4, are located within a
shield in the form of a hollow, inverted truncated pyramid 7. The
peripheral surface of the distribution drum 10 is recessed or
provided with grooves arranged in a pattern depending upon the
distribution of powder to be obtained on the web 2. The recesses,
which may be of depressed-mammilated form, may contact one another
or be narrowly spaced, and are so dimensioned as to receive a
single powder grain or a plurality thereof as desired. A number of
interchangeable drums may be provided, each having a respective
different pattern so that by making a suitable selection from the
drums available a desired particle distribution may be
obtained.
The circumferential and axial spacings of the recesses and their
distribution, which may be as desired, determine the distribution
of the powder grain or of the powder grain accumulations, whilst
the selection of the depth of the recesses makes it possible to
provide the powderous layer of the desired thickness. Heating and
cooling devices (not shown) make it possible to keep the surface of
the drum 10 at a predetermined temperature or to alter this in a
predetermined manner. Ducts passing through the drum body are
especially suitable and may conduct a coolant, for example brine,
or a heating agent, for example oil. The drum 10 rotates in the
counter-clockwise direction (with reference to the drawing).
Initially, the loose layer of powder falling upon the drum from the
plate 5 reaches the doctor roller 8. The doctor roller 8 has a
heavy core 13 and a resilient, foamed material sleeve 12, which
under the effect of the weight of the core, distributes the powder
layer among the recesses in the surface of drum 10. Surplus powder
is removed by the doctor blade 14 of the stroking doctor 9, the
edge of the blade 14 coinciding with the peripheral surface of the
drum 10, that is the surface in which the recesses are formed,
ignoring the depth and distribution of the recesses.
The web 2 of a textile material is fed in the direction firstly
through a damping device 15 to eradicate vibration and then over a
spherically surfaced expansion roller 17 to stretch the web. The
web is then carried over a heated pressure roller 18 revolving on
or with a shaft 19 and heated by conventional means, for example
ducts conducting heated oil, such ducts not being shown in the
drawing. The shaft 19 of the pressure roller 18 is either under
spring pressure or the bearings supporting it are adjustably
arranged in such a way that the pressure roller 18 applies the web
2, with an adjustable pressure against the peripheral surface of
the drum 10. Contact of the web 2 with the drum 10 leads to
transfer of the powder retained in the recesses formed in the
surface of the said drum onto the web. No relative movement takes
place between the web and the drum 10 between the points where the
web and drum 10 meet and separate. In addition, the powder
particles are securely trapped between the peripheral surface of
drum 10 and the web itself so that the powder is not subject to
external forces acting in the space surrounding the apparatus, thus
the thickness and distribution of the coating is unchanged by
draughts, convection currents or vibrations for example. A second
pressure roller 20, which is likewise heated and revolves about or
with its shaft 21 in the clockwise direction, serves to separate
the web 2 from the drum 10. As will hereinafter be explained, the
coating has become bonded to the web 2 in the time taken by the web
to pass from roller 18 to roller 20 and consequently the separation
of the web from the drum 10 does not dislodge the powderous
coating.
It is therefore possible, with the aid of infra-red heating means
22, to carry out the plastification of the powder grains or powder
grain accumulations absorbed by the web 2. After this, the web 2
enters the nip 23 between the calendar rolls 24, 25 and is
withdrawn at 27 after deflecting and, if necessary, cooling on the
roller 26.
The drawing shows only those devices which are necessary to coat
any desired web with a coating of discrete particles evenly and
with constant coating thickness. However, the calendar represented
at 23 to 25 could be used to feed further materials, which are to
be cladded with the coated web. Further, the web 2 may be coated on
both sides with the discrete particles and then be interposed as a
lining material between two webs of other materials. The use of
such additional and, what is more, known methods is not precluded
by the diagrammatically described and represented exemplified
embodiment, but the introduction of such processes into the method
to be performed in accordance with the invention introduces the
advantage of simplified technical performance and a higher economy
since the number of heatings and/or coolings can in this way be
substantially reduced.
Because the drum 10 can be brought to a temperature at which the
powder, irrespective of its chemical constitution, does not possess
any adhesive effects, or only such weak ones that the powder is
incapable of adhering to surface parts of the drum 10, the
conveying and distribution process can be performed without the
disadvantages engendered by this property becoming manifest. Exact
details regarding the temperature of the distribution drum 10 have
been given above. The relationships thereby given between the
points at which the drum 10 receives the powder and the drum 10 via
web 2 contacts the roller 18, change however in the regions of this
zone of contact. The roller 18 is normally heated to about
200.degree. C and kept at this temperature. The temperature of the
web 2 increases correspondingly so that the powder grain present in
the recesses of the drum 10 are brought rapidly to temperatures at
which they develop strong adhesive properties. This leads to a
transfer of the individual grain or grain accumulations from drum
10 to the web 2 in exactly the same pattern as the powder grains or
grain accumulations form when lying in the depressions of the drum
10. The drum 10 is maintained at a lower temperature than the web
and there is thus no tendency for the particles to adhere to the
drum. The effect of gravity on the loose particles carried on drum
10 as this drum rotates can be compensated for by increasing the
height at which roller 18 is disposed. In practice the dimensions
of the shield 7 in the peripheral direction can be less than those
shown, which have been exaggerated for illustration purposes.
It is impossible for the grains to change their position once they
are located between the web 2 and the drum 10 because they are
firmly trapped in position. Not until the web, by means of the
pressure roller 20, (likewise heated to about 200.degree. C) is
removed from the surface of the drum 10 does the enclosure of the
absorbed powder grain on both sides cease. Even then, the tendency
is for the grains to adhere to the web because of the presence of
the heated roller 20. Subsequently the grains are carried on the
upper side of a horizontal strand of the web tensioned between
rollers 20, 24. At this stage the powder is heated by infra-red
heaters 2.
Thus, due to the measures taken, it is ensured that the
distribution of the powder particles on the web corresponds to the
pattern of recesses on the drum 10. In this way, the product leaves
roller 27 in a formation which exactly corresponds to the
respectively existing operating regulations.
It should be appreciated that the particulate material may be
transported on the drum 10 through the coating station which is
defined between the nip of the drum 10 and the roller 18 at a
temperature less than the ambient temperature in those instances
where the particulate material is of a characteristic which may
make this desirable. At the coating station, the particulate
material is advantageously brought into contact with the backing
material at about the plastification temperature of the particulate
material. Temperature control means (e.g. electrical or liquid
heaters not shown) are usually provided for controlling the
temperatures of the pressure rollers 18 and 20 and in some
instances a similar temperature control element is connected to the
drum 10 for regulating its temperature. The drum 10 may be
maintained at a temperature below ambient temperature and the
temperature of the pressure rolls maintained at about the
plastification temperature of the particulate material.
* * * * *