U.S. patent number 3,854,441 [Application Number 05/334,747] was granted by the patent office on 1974-12-17 for apparatus for applying barrier coating substances to sheet materials.
This patent grant is currently assigned to Bolton-Emerson, Inc.. Invention is credited to George C. Park.
United States Patent |
3,854,441 |
Park |
December 17, 1974 |
APPARATUS FOR APPLYING BARRIER COATING SUBSTANCES TO SHEET
MATERIALS
Abstract
A barrier coating of the high viscosity "hot melt" class is
applied with high uniformity to a moving web by means of a coating
apparatus which is capable of operating at speeds as high as 1,500
feet per minute utilizing "hot melt" compounds of viscosities
ranging as high as 100,000 c.p.s. The coating fluid in a heated
condition is applied from a coating head consisting of a tubular
body formed with an elongated aperture over which the web is
passed. The coating fluid is under relatively high pressures of
varying intensity. Pressure change along the elongated aperture is
controlled by regulating web pressure. Multiple tensioning means
are arranged at two opposite sides of the coating tube. One
tensioning device engages the web at it approaches the coating head
and acts initially to exert cross tension and stretch the web
sufficiently to overcome variations in caliper and web length. A
second tensioning device exerts linear tension to force the
transversely stretched web uniformly against the coating tube with
sufficient web pressure to equalize and balance pumping pressure of
fluid all along the coating aperture. Required web pressures of a
magnitude necessitating linear tension in excess of the tensile
strength of any given web is provided by means of a web press roll
adjustably supported in rolling contact with the web immediately
above the elongated tube aperture. The web press roll is adjustable
both vertically and horizontally to vary its position relative to
the elongated tube aperture.
Inventors: |
Park; George C. (North Reading,
MA) |
Assignee: |
Bolton-Emerson, Inc. (Lawrence,
MA)
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Family
ID: |
26947067 |
Appl.
No.: |
05/334,747 |
Filed: |
February 22, 1973 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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259072 |
Jun 2, 1972 |
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48660 |
May 15, 1970 |
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806473 |
Mar 12, 1969 |
3556832 |
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806040 |
Mar 6, 1969 |
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33567 |
Jan 3, 1964 |
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Current U.S.
Class: |
118/34;
118/410 |
Current CPC
Class: |
D06B
1/08 (20130101) |
Current International
Class: |
D06B
1/00 (20060101); D06B 1/08 (20060101); B05c
005/02 () |
Field of
Search: |
;118/33,34,410,411,122,8,6 ;226/39,195 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: McIntosh; John P.
Attorney, Agent or Firm: Hamilton; Munroe H.
Parent Case Text
This application is a continuation-in-part of Ser. No. 259,072,
filed June 2, 1972, now abandoned; which in turn is a
continuation-in-part of Ser. No. 48,660, filed May 15, 1970, now
abandoned; which in turn is a division of 806,473, filed Mar. 12,
1969, now U.S. Pat. No. 3,556,832; which in turn is a
continuation-in-part of Ser. No. 806,040, filed Mar. 6, 1969, now
abandoned; which in turn is a continuation of Ser. No. 335,607,
filed Jan. 3, 1964, now abandoned.
Claims
I claim:
1. Apparatus for applying a viscous coating of the hot melt class
to a web of material, said apparatus comprising a frame, a supply
roll member for supporting a wound roll of the material at one end
of the frame, winding roll means mounted at an opposite end of the
frame, power driving mechanism for actuating the winding roll and
drawing off a web of the material at a desired rate of travel, a
coating tube arranged in the frame below the path of said web to
engage the web, said coating tube being constructed with a curved
upper side and having an elongated discharge aperture formed along
said upper side and lying within the confines thereof, said
aperture having high lead-on edge and a low lead-off edge, tension
roll means located both in advance of, and in rear of, said tube on
said path for exerting tension in the web and guiding the web in an
arcuate path of travel over said curved upper side and over said
lead on and lead-off edges, a roll mount structure, a press roll
rotatably supported in the roll mount structure above the coating
tube in rolling engagement with the web and forming a pressure nip
with said tube, and said press roll having its axis of rotation in
rear of said lead on edge directly above said lead-off edge and
lying in a vertical plane which passes through the lead-off edge of
the elongated discharge aperture.
Description
The present invention relates to apparatus for applying a barrier
coating substance to sheet materials of the class including paper
webs, films, foil, fabrics, and the like. More particularly, the
invention is concerned with a coating apparatus of the class in
which a coating tubular coating head including an elongated
discharge aperture is employed. It is contemplated that the coating
substance may be applied as a single coating or in the form of
successive coatings, one applied to function as an outer protective
surface on one or both sides of a singlr layer of material. The
coating substance may also be employed as an adhesive or bonding
agent for laminating two or more webs of material together.
In coating a web of material with a slotted coating tube through
opposite ends of which a high viscosity coating fluid is forced, a
commonly experienced difficulty is failure to apply the coating in
a uniform thickness all the way across the web. This may occur
largely because of pressure drop toward the center of the tube due
to increased friction. As a result, greater internal pumping
pressure is exerted at the outer ends of the tube aperture or slot
than at the center.
While such difficulties are subject to some degree of control when
using ordinary solvent and emulsion-type coating materials applied
at relatively low flow rates, a much greater problem is present
when dealing with high viscosity materials discharged at relatively
high pressures to provide increasing higher flow rates. Under such
conditions greater web pressure, normally induced by increasing
linear tension, becomes necessary to maintain the web against the
coating tube or head and for some coating operations, the
requirement for added tension may exceed the tensile strength of
the web with consequent breaking.
A further condition which manifests itself is the tendency for high
viscosity material supplied at higher flow rates to displace any
portions of the web which are slack or which are subject to
bariations in caliper or length. Furthermore, substantially
increased tension forces exerted linearly of a web having a slack
or non-uniform portions may tend to draw the web undesirably and in
this way also unsatisfactory coating will occur.
It is, in general, therefore, a chief object of this invention to
deal with the problem indicated above, and to provide an improved
apparatus for applying barrier coating substances of relatively
high viscosities utilizing a tubular type coating head. It is a
further object of the invention to devise a coating apparatus which
includes novel means for controlling web pressure and web tension
in combination with a tubular type coating head and to utilize the
coating apparatus in coating thermoplastic compounds of the class
commonly referred to as "hot melt" compounds which may have
relatively high viscosities in a viscosity range running as high as
100,000 c.p.s.
Another object of the invention is to devise apparatus for applying
high viscosity coatings to webs which are subject to variation in
caliper and length in order to insure application of highly uniform
layers and elimination of streaks or lines resulting from particles
being collected in the coating equipment.
Another object of the invention is to provide a coating apparatus
by means of which web speed and pumping rates may be synchronized
and a continuous indication of both web speed and pumping rates may
be visually presented to a machine operator so that a more
efficient coating operation may be realized.
Still another object of the invention is to provide a modification
of the coating apparatus of the invention in which a means for
imparting internal tension to a web is provided.
The nature of the invention and its other objects and novel
features will be more fully understood and appreciated from the
following description of a preferred embodiment of method and
apparatus selected for purposes of illustration and shown in the
accompanying drawings in which:
FIG. 1 is a plan view illustrating schematically a web and
apparatus employed in coating the web with a high viscous coating
material;
FIG. 2 is a side elevation view further illustrating a web moving
through the coating apparatus of the invention and particularly
indicating multiple tensioning means;
FIG. 3 is a front elevational view of the apparatus shown in FIG.
2;
FIG. 4 is a vertical cross sectional view showing details of the
tubular coating head and a web in a coating position;
FIG. 5 is an enlarged vertical cross sectional view further
illustrating portions of the coating head and web of FIG. 4;
FIG. 6 is a fragmentary cross sectional view of the applicator head
taken approximately on the line 6--6 of FIG. 9;
FIG. 7 is a cross sectional view of a tubular component shown
removed from its supporting structure;
FIG. 8 is a fragmentary elevational view of the coating head shown
with heating means associated therewith;
FIG. 9 is a cross sectional view taken on the line 9--9 of FIG.
8;
FIG. 10 is a cross section taken approximately on the line 10--10
of FIG. 9;
FIG. 11 is an exploded view of the coating head components,
portions of which are indicated fragmentarily;
FIG. 12 is a fragmentary detail plan view illustrating a web of
paper in an operative position relative to the coating tube;
FIG. 13 is a plan view illustrating diagrammatically power driven
components of the coating apparatus connected in interlocking
driving relationship for synchronizing web speed and pumping rates
in a visually indicated manner;
FIG. 14 is a cross section illustrating diagrammatically a multiple
coating operation;
FIG. 15 is a detail cross sectional view of a modified form of
coating head apparatus which includes a special web press roll
member;
FIG. 16 is a fragmentary elevational view further illustrating the
coating head and web press roll apparatus of FIG. 15;
FIG. 17 is a detail cross sectional view illustrating
diagrammatically a web fibre ironing step;
FIG. 18 is a diagrammatic view illustrating an operator's chart for
one specific coating operation;
FIG. 19 is a plan view illustrating schematically a web coating
apparatus having an internal tensioning and clutch mechanism for
regenerative braking;
FIG. 20 is a perspective view illustrating diagrammatically the
apparatus shown in FIG. 19;
FIG. 21 is a side elevational view of a coating machine in which
the apparatus of FIG. 19 is contained;
FIG. 22 is a side elevational view of an opposite side of the
coating machine of FIG. 21, and
FIG. 23 is a fragmentary detail view of portion of the clutch and
gear mechanism shown in FIG. 21.
As earlier noted, the coating method and apparatus of the invention
in one preferred embodiment is designed to handle "hot melt"
materials of the class which may require heating to temperatures as
high as 400.degree. F and which may occur in a viscosity range
running as high as 100,000 c.p.s. The invention will, therefore, be
described with reference to the use of these high viscosity coating
materials although it should be understood that this is not done in
a limiting sense and various other classes of coating materials may
be employed in the invention method.
With this preferred embodiment of the invention method, it is
contemplated that webs may be coated in a range of widths of from
15 to 85 inches up to 200 inches at speeds running as high as 1,500
feet per minute and providing coating weights of from 2 lbs. up to
40 lbs. or more. Coating may be applied to cover one side or two
sides of a web and the method may also be employed to coat,
laminate with a second web, and again coat, all in one pass through
the machine.
In carrying out the method in its preferred form and handling high
viscosity coating materials, I have discovered that I may employ
specially controlled web tensions and web pressures in combination
with a tubular type coating head and I have devised as one
important feature of the invention multiple tensioning means
arranged at two opposite sides of the coating head in relatively
depressed positions.
The multiple tensioning means acts on the web as it leaves a supply
roll and approaches the coating head under linear tension. Then
just before and just after the head transversely directed
tensioning forces stretch the web transversely in sufficient degree
to overcome variations in caliper and length of the web.
This cross tensioning step of the invention is essential to
successful use of linear tension and linear tension as further
exerted through the multiple tensioning means acts to force the
transversely stretched web uniformly against the coating head with
adequate pressure to equalize and balance variable pumping
pressures of high viscosity fluid along the coating head and thus
the problem of pressure drop from friction may be controlled.
I have further discovered that in some coating operations, where
very high viscosities and high flow rates may require web pressures
of a magnitude necessitating linear tension in excess of the
tensile strength of the web, I may provide additional web pressure
at the coating head by employing a special web press roll supported
in rolling contact with the web immediately above the coating head
aperture and adjustable both vertically and horizontally relative
to the coating head.
I have futher determined that in controlling web tension and web
pressure in the manner disclosed, it is important to maintain web
speed and pumping rate in constantly regulated relationship to one
another in order to apply precisely controlled coating weight to
the web.
In this connection, I have still further devised a novel
interlocking drive mechanism for actuating both web winding means
and fluid pumping means so that web speed and pumping rate in
pounds per minute may be synchronized in a desirable manner.
I have still further devised a unique flowmeter and indicator
apparatus by means of which the synchronized web speed and pumping
rate are visually indicated to an operator at all times. For use
with the indicator apparatus, I have in addition also provided
novel chart means for monitoring machine operation in accordance
with a desired coating weight to be applied.
Considering in more detail the apparatus of the invention, I employ
a coating head having a tubular coating element formed with an
elongated aperture. Heated coating fluid is forced through opposite
ends of the tube under pumping pressure. The heated coating fluid
is discharged through the elongated aperture from a confined space
which is substantially sealed at one side. Sealing is accomplished
by continuously advancing portions of the web under tension and in
overlapping relation to opposite ends of the elongated aperture so
that material is coated on the web at points inside of the edges of
the web at all times.
Attention is directed to FIG. 1 wherein I have illustrated a supply
roll E from which a web of material W is drawn off by winding roll
means and subjected to a coating operation to provide a coated
material W1 having a coating L at the underside thereof. The
material W may consist of a cellulosic web and the coating may
consist of a thermoplastic coating substance applied from the
heated tubular coating head generally indicated by arrow T and
including a tubular coating element T1. As suggested
diagrammatically in FIG. 1, heated coating substance of heavy
viscosity may, for example, be delivered from a supply source S by
a pump P to the coating element T1. A heating medium such as a
source of steam at H is arranged to provide a circulation of heat
to a heat-conducting body in the tubular coating element T1 through
inlets H1 and H2 and an outlet H3. These components are further
illustrated in FIG. 3 wherein the pump P and a container for
coating substance are shown supported in bracket members 4 and 6 on
frame side 2.
The web W is continuously advanced at desired speeds by winding
roll means as R. R1 and R2 indicated at the upper right hand side
of FIG. 1. Also provided is a variable speed power drive for
controlling the web speed through the machine. The variable speed
power drive may, for example, include a variable speed motor M
which drives a shaft M1 having a sprocket M2 and chain M3 in turn
meshing with a sprocket M4 on a shaft M5 of winding roll R.
In accordance with the preferred embodiment of the invention, I
combine with the web winding and coating head means referred to
special multiple tensioning means more clearly shown in FIG. 2 and
constituting an important and essential feature of the invention
method. The multiple tensioning means includes tensioning devices
which are so designed and combined with the coating head T that
both variation in web caliper and length as well as variation in
pumping pressure at the coating head may be simultaneously dealt
with and controlled.
Attention is directed to FIG. 2 wherein it will be observed that
the web W is drawn off from the supply roll E under a tension which
is induced by the power driven winding roll R at R/R1 and braked at
R3/R4 which may be of any given intensity common to typical winding
speeds.
In addition to this winding tension, I provide for additional
tensioning of the web by means of multiple tensioning devices
located at either side of the coating head T and in depressed
positions such that tensioning forces are exerted from points below
the top of the coating tube T1 in both cases.
The multiple tensioning devices are shown in detail in FIGS. 2 and
3 together with the coating head T and web guiding means. As shown
in FIGS. 2 and 3, a roll stand V supports a roll of material from
which the web W is continuously drawn off by a nip R/R1 passing
through the braking nip R3/R4 and then over preheating roll R4.
These rolls are supported between frame sides 2 and 2' having
extensions 2a and 2b and between the extensions 2a and 2b are
supported in a fixed position opposite ends of coating head T.
Located in the frame extension at the righthand side of the coating
head T as viewed in FIG. 2, is one of the multiple
tension-compensating devices of the invention consisting in a cross
tensioning roll assembly F1 and located at the opposite side of the
coating head T is a second linear tensioning roll assembly F2.
The cross tensioning roll assembly F1 includes as a principal
component a rotating bowed expander roll R5 which has opposite
extremities received in bearings in a roll stand 100. The expander
roll extremities are provided with independent vertical adjustment
means 102 for raising and lowering the roll R5. Also provided are
lateral adjustment means for moving the roll R6 into and out of
skewed position. Operating wheels RW1 are fixed to control rods as
105 having bevel gears 106 for facilitating manual adjustment of
the roll R5.
It is pointed out that the axis of rotation of roll R5 is located
substantially below the top of coating head T but is in close
proximity to this member so that as a result the web W is subjected
to cross tensioning and transverse stretching forces and almost
instantly while in a stretched state the stretched web moves over
and around the coating head T.
In thus subjecting the web to cross tensioning forces I may vary
the stretching action by raising and lowering the roll R5 as may be
required from time to time and I may also increase the cross
tensioning action by moving the roll R6 laterally into and out of
skewed positions and I may also employ additional rolls in a skewed
position.
The linear tensioning roll assembly F2 includes a roll member R6
rotatably mounted in a roll stand 108 in suitable bearing members
which can be adjusted toward and away from the coating head T by
means of an operating wheel RW. The linear tensioning roll R6 is
located with its lowermost peripheral portion occurring well below
the top of the coating head T so that a linear tensioning force can
be exerted downwardly of the coating head T and more importantly
while the web is in a cross tensioning or stretched condition
constantly controlled by the bowed expander roll.
I have determined that by combining the multiple tensioning means
noted with the coating head T in the relative positions to one
another described, a novel and important multiple tensioning effect
is realized. This multiple tensioning acts on the web W as it
leaves the supply roll E and approaches the coating head T and
operates initially to exert cross tension force of a magnitude
which may stretch the web transversely in sufficient degree to
overcome variation in caliper and length of the web.
The controlled cross tensioning step of the invention is, as
earlier noted, essential to successful use of linear tensioning of
the web and makes it possible for linear tension as further exerted
by the assembly F2 to force the transversely stretched web
uniformly against the coating head with adequate pressure equalize
and balance varying pumping pressures developing along the coating
head.
In controlling web tension and web pressure in order to overcome
difficulties arising out of the use of high viscosity coating
material utilized at relatively high flow rates there may develop
conditions where the necessary web pressure requires a web tension
which exceeds the tensile strength of the web to be coated and
frequent breaking or tearing can occur.
To deal with this problem, I have devised auxiliary web press roll
means for increasing web pressure against the coating head while
still regulating linear and cross tensioning in the web itself. A
preferred web press roll means is illustrated in FIGS. 15 to 17
adjustably mounted above the coating tube T1, and includes
essentially a web press roll 130 and roll-mount means in which the
roll is adjustably supported for rotative movement in varying
positions relative to the coating tube T1.
In the roll and roll mount structure referred to, there is included
a shaft 132 together with means for adjusting the roll and shaft
forwardly and rearwardly relative to the coating head T1 as
indicated by the horizontal arrow in FIG. 15. I also provide means
for adjusting the position of the press roll and its shaft 132
upwardly and downwardly as suggested by the vertical arrow in FIG.
15, in order to exert varying degrees of pressure against the web W
in any desired position of horizontal adjustment over the coating
tube T1.
As one desirable form of roll mount means for accomplishing this
dual adjustment, I may employ a pair of pneumatic cylinders 134 and
136 adjustably mounted at opposite sides of the machine on the
frame sides 2 and 2' for movement forwardly and rearwardly into
desired positions of lateral adjustment, as indicated in FIG. 15.
At their upper extremities, the pneumatic cylinders may be either
pivotally or slidably supported. Suspended from respective plunger
elements of the pneumatic cylinders 134 and 136 are elongated
bearing blocks 133 and 135, better shown in FIG. 16. The elongated
bearing blocks 133 and 135 are slidably disposed on horizontal
guide rods as 138 and 140 which may be yieldably secured to
adjacent portions of the frame sides 2 and 2'. Formed through ends
of the elongated bearing blocks 133 and 135 are openings for
receiving therethrough opposite extremities of the shaft 132.
By means of the mounting arrangement described, it will be readily
seen that in a coating operation where the web W is required to be
pressed against the coating head T1, the roll 130 and shaft 132 may
be adjusted into any desired position of horizontal adjustment and
thereafter pressure may be exerted through the pneumatic cylinders
in any desired degree to force the roll 130 against the web W.
It will be observed that in a vertically centered position of the
press roll over the coating tube T1, the axis of rotation of the
press roll and the central axis of the tube T1 will lie in a common
vertical plane. If, however, the press roll is moved forwardly or
rearwardly, its axis of rotation will be in a vertical plane which
occurs at one side of and in spaced relation to the common vertical
plane noted above, and greater pressure may then be exerted against
one side or the other of the coating head slot.
I have determined that for many highly viscous coating materials,
and particularly viscous hot melt substances of the elastomeric
type, it is important to control the adjustment of the press roll
relative to the coating head slot, and I have found that
positioning the web press roll in a forwardly located position,
i.e., from right to left of the coating head T1, as shown in FIG.
15, and then exerting web pressure, provides in many cases clearly
superior coating results, and particularly so, where in an
instance, the axis of the press roll is positioned to lie in a
vertical plane which passes through or very close to the lead-off
edge of the coating tube slot.
I have further found that in coating with some extremely difficult
coating materials, it is essential to use the combined horizontal
and vertical adjustment of the web press roll in order to obtain a
satisfactory coating application. In thus adjusting the web coating
roll, I may desire to use various other mounting arrangements with
adjustments and I may desire to positively drive the press roll or
to vary its diameter through a range of sizes.
I find that by thus combining web press roll pressure with cross
tensioning and limited linear tensioning, the problem of web
breaking can be avoided with uniformity of coating thickness being
effectively maintained, and I may also desire to employ the web
press roll for various other coating requirements.
Considering in further detail the coating head assembly T, there is
included in this assembly a tubular element T1 having a specially
formed elongated aperture and adjacent land surface by means of
which a precisely metered quantity of coating substance supplied by
the pump P may be applied to a web and desirably smoothed out.
Numeral 40 denotes the aperture which is more clearly shown in
FIGS. 4--1 inclusive and is located at the upper side of the
tubular element T1.
The tubular element T1 is constructed as a cylindrical body which
is open at opposite ends and along its upper side. There is thus
defined a confined space having an aperture 40 as shown in FIG. 7.
Opposite edge portions of this aperture 40 are adapted to be
secured in circumferentialy adjustable relation to one another by
means of adjustment screws as 42 located transversely through
opposite sidewall sections as shown in FIGS. 4 and 7. By adjusting
these screws the width of the elongated aperture 40 may be varied
as desired.
I also provide between these adjustable sidewall sections filler
strips as 44 (FIG. 6) which operate to close the aperture 40 at
opposite ends of the tubular element so that the quantity of a
coating to be applied from the aperture 40 may extend over a
greater or lesser area.
The aperture 40 is further defined by a special metering edge
construction including a relatively high lead-on edge 46 over which
a web of material is led to the coating substance, and a relatively
low lead-off edge 48 over which the web and an applied layer of
material is led away.
It is pointed out that when a web is moving over the tube T1 the
relative difference in height between the lead-on edge 46 and the
lead-off edge 48 provides for the formation of a short restricted
passageway into which freshly coated underside portions of the web
may move without the coating being drawn across a sharp edge. It
will also be observed that this restricted passageway tends to
become larger if the flow of the coating substance extruded through
the aperture 40 increases.
In combination with this relatively lower lead-off edge
construction, I have further provided a novel land surface
construction which is denoted by numeral 50 more clearly shown in
FIGS. 6 and 7 and consisting of a relieved relatively flat area
which extends away from the aperture for a short distance to become
terminated at a recessed portion 52. This land surface is designed
to smooth and level a coated surface of a web passed thereover and
to set the coating substance firmly against the web.
Another feature of the invention is the provision of pressure
equalizing means for the member T1 embodied in the construction and
operation of the tubular coating apparatus T as shown in greater
detail in FIGS. 4-11, inclusive. As noted therein member T1 is
located in a special mounting assembly supported at the front of
the frame as shown in FIG. 3 in bearing plates 15, 17.
Included in this assembly is a heat conducting bed tube 15 which,
as shown in FIG. 11, is formed along its upper and lower sides with
curved recesses in which are supported respectively the tubular
coating device T1 and a second tubular member T2. Opposite ends of
members T1, T2 and bed tube 16 are received through collar members
as 18 and 20 adapted to be bolted to the bearing plates 15 and 17.
Secured outside the ends of the bed tube 16 and tubes T1 and T2 are
closure members 22 and 24.
As will be observed from an inspection of FIGS. 9 and 11, these
closure members 22 and 24 are formed with internal passageways 22a
and 24a which communicate with tubular members T1 and T2. The
closure members 22 and 24 are further formed with central plug
sections 22b and 24b which are constructed and arranged to fit and
seal respective opposite ends of a steam chamber 16a of the heat
conducting member.
By means of this arrangement steam for heating the bed tube 16 may
be introduced through inlets H1, H2 into a steam chamber 16a and
removed from an outlet H3. There is thus provided a means of
transmitting heat to such of the tubes T1 and T2 in order to
maintain at a desired temperature a body of coating substance in
the tubes T1 and T2.
As shown in FIG. 3, a supply of the coating substance is pumped
from the supply source S by pump P through a feed pipe 30 (FIG. 9)
into passageway 22a. Valve V.sub.1 opens and closes the feed pipe
while V.sub.2 provides for recirculating material through pump and
strainer. A portion of the coating substance passes from passageway
22a into the tube T1 while another portion of the coating substance
passes through the tube T2 into the passageway 24a and then into an
opposite end of tube T1. With this arrangement, it will be observed
that there is no opportunity for pressure to drop from frictional
losses in forcing material into tube T1.
A further feature of the coating means of the invention is the
arrangement of parts in the tube T1. As noted in FIGS. 6 and 7, the
tube T1 is split along its upper side and formed with a kerf K at
its bottom side so that the split may be opened or closed by
turning adjustment screws 42. The pressure thus exerted squeezes
the filler strips 44 to prevent escape of liquid material at these
points. Opposite ends of T1 are further fitted with sealing rings 0
which seal against end closure members 22 and 24.
In some coating operations where conditions tend to increase the
likelihood of streaks or ridges in an applied coating, I may desire
to combine with the coating tube T1 a special coating leveller
device which is illustrated in FIG. 4. This device includes an
adjustable block 120 mounted in close proximity to tube T1 and
having adjustably secured therein an L-shaped bar 122 mounted over
a tube 124. Formed in the L-shaped bar along one edge is a V groove
126 in which is loosely contained a levelling rod 128. I find that
this levelling device may be set to engage a freshly coated web and
the loosely disposed rod will function to spread out small
quantities of fluid which accumulate as a small excess body 130 all
along back of the rod and this excess body tends to provide a
uniform levelling action of a desirable nature.
In carrying out the method of the invention, a supply of high
viscosity heated coating substance is pumped into the tubes T1 and
T2 to provide uniform pressure all along tube T1. The coating
substance is constantly maintained at a desired temperature by the
heat conducting tube 16. At the same time, the web W of paper is
guided into contact with a nip roll R3 and a preheating roll R4 and
then through the multiple tensioning means and coating head T as
earlier described. At this point the web is caused to move through
an arcuate path of travel which provides for a predetermined amount
of contact of "wrap-around" of the paper with respect to the tube
T1 and which may extend over an arc of 45 degrees or more. A
desired tension is exerted in the web and pressure is exerted by
the web against the coating head slot. If the tension requirements
cause breaking of the web, then the press roll arrangement of FIGS.
15 to 17 is utilized.
It is pointed out that the wrap-around of the web may be controlled
to not only convert the tube T1 into a closed container with
resultant pressure equalization, but may also provide a highly
beneficial effect in laying down heated fibres of rough surfaced
webs immediately prior to application of coating. This prevents
fibres from remaining erect and penetrating the coated layer to
permit wicking and thus destroy the barrier properties of the
coating. This fibre-ironing action is illustrated diagrammatically
in FIG. 17 in which fibres 120 in a web W6 are laid down and held
while coating layer 122 is applied from coating tube T1.
As shown in FIG. 12, for a given width of a web W which is to be
coated, the length of aperture 40 is controlled by use of filler
pieces 44 so that opposiste edges of the web W will overlap the
filler strips and when held under a suitable tension will tend to
seal the area of elongated aperture 40 and constitute the space
within the member T1 as a closed volume. By this means uncoated
strips may be left on the web with a minimum of difficulty.
In accordance with a preferred form of the invention, the pump P is
regulated so that a substantially constant rate of flow of coating
substance is delivered to the member T1 and at a predetermined
pressure which is of a magnitude such that it exceeds slightly the
radially inwardly directed force component of the tensioned web of
paper W. Pressure thus induced raises the paper a distance above
the aperture 40 which generally corresponds to the thickness of a
layer of coating substance desired to be applied to the underside
of the paper. In this way, I am enabled to apply only a desired
amount of coating substance and the web is never "flooded" and
therefore does not require scraping with a doctor blade.
As this metered quantity of coating is removed from the top of the
body of coating substance in opening 40 and applied to the web, it
is almost instantly moved in over the relatively low lead-off edge
48 and then through the short restricted passageway comprised by
the land surface 50 and the moving web itself. While passing
through this passageway, the coating is levelled, compressed and
smoothed against the land surface 50 and set into the paper to
eliminate any irregularities. A desirable result of this passageway
is that small particles which may occur in the coating substance
are carried off in the coated layer without collecting on the
lead-off edge to cause streaking.
In thus providing the passageway noted, I have found that improved
results may be obtained by having the lead-off edge 48 spaced lower
than the lead-on edge 46 a distance lying in a range of from .005
to .007 inches. A typical coating weight resulting from a pumping
rate employed in forcing the coating material through the elongated
aperture 40 may be expressed as quantity of material applied, e.g.,
as 5 pounds per thousand square feet for a 60 -inch web travelling
at a rate of 600 feet per minute. This provides a coating thickness
of approximately 0.001 inches. An optimum land surface is one
extending for a distance of one-eighth inch between the lead-off
edge 48 and the point of recess which forms the surface 52. The web
is in contact with the coating tube T1 a total not exceeding one
and three-quarter inches in the direction of its movement.
The web with coated layer L leaves the tube T1 somewhat abruptly at
the point of the recessed part 52 after having passed along the
land surface 50. Further movement is in a straight path of travel
to the roll T6 for a short interval of time after which the web is
turned and guided in a reversed path of travel. This reverse path
of travel coming immediately after the coating step tends to extend
and stretch the coating L in a desirable degree. After having thus
been turned the web and the stretched coating thereon passes to
roll T1 and then to roll R which is constantly cooled to a desired
temperature whereby the layer L of coated substance may be shock
chilled and set to a desired condition while still in a relatively
stretched state.
The combined effect of reversing the web to stretch the layer L and
almost immediately thereafter shock chilling the partially set or
hardened material prevents any tendency for curling of the paper to
develop as the layer L becomes fully conditioned. As a result, I
may, by controlling the stretching of the layer and its time of
setting provide a paper stock which will remain flat in sheet
form.
While satisfactory results for some coating operations may be
achieved using the equipment as described above, I have determined
that in many cases where high viscosity coatings are applied at
relatively high flow rates, a more precise control of web speed and
pumping rates is required for most efficient machine operation.
With this in mind, I have further devised a method and means for
synchronizing web speed and pumping rate in pounds per minute in an
accurately controlled manner.
Attention is directedd to FIG. 13 wherein I have illustrated an
arrangement for interlocking the actuating means for a pump P1 with
the drive means for winter rolls R10, R11, R12. As shown in FIG. 13
a variable speed motor 140 drives a shaft 142 having a sprocket 144
and a chain 146. The chain 146 meshes with a sprocket 148 on shaft
150 which carries winding roll R10. A sprocket 152 on shaft 150
drives a chain 154 which in turn drives a sprocket 156 on a shaft
158. The shaft 158 is connected to a variable speed transmission
member 160 in turn connected to shaft 162 coupled to the pump drive
164. By means of the arrangement described, the pump rate in pounds
per minute can be set to a desired value for any given web speed
and the two will then move in constantly maintained synchronized
relationship.
I find that this synchronized operation performs very
satisfactorily with the multiple web tension and web pressure
controls earlier described to control coating weight uniformly.
I have also devised special indicator means including a flow-meter
170 connected into the pumping line to the tube T1 as shown in FIG.
13 and having a connection to an indicator device 172 which
automatically indicates pumping rate in pounds per minute in
response to changes in the flow-meter readings. Also combined with
the indicator device 172 is a second indicator means 174 which, by
means of a suitable tachometer device, senses the rate of speed of
the shaft 150 and translates the speed into a reading of feet per
minute of travel of web W4. Thus it affords a convenient and
extremely useful indicator for visually indicating to a machine
operator readings in web speed and pumping rate.
In a typical instance of carrying out a coating operation with
mechanism for synchronizing both web speed and pumping rate as
described above, a roll of material is put in place in the roll
stand V. A web of the material is drawn off at a desired web speed
and limited tension is exerted by the multiple tensioning means of
the invention until the web runs through without the edges being
skewed. Then the pump speed is set to operate at a rate which will
furnish a required coating weight in pounds per square feet.
Thereafter linear tension is increased gradually until the
longitudinal cross section profile of the web is uniform. This is
determined by blanking or cutting out small samples of the coated
web and weighing these samples to check on uniformity. Finally with
web speed, linear tension and pumping rate adjusted correctly,
cross-tensioning is adjusted to provide a uniform cross section
profile as determined by cutting samples a second time and checking
their weight. In FIG. 1, one form of cutout samples Y are indicated
diagrammatically to illustrate these profile measuring operations.
With these conditions having been established, I may increase or
decrease the pumping rate to obtain heavier or lighter coatings as
desired with uniformity being preserved.
I also provide chart means for use with the indicator device
described and one typical chart is illustrated in FIG. 18. As shown
therein the chart presents tabulated data in the form of pounds of
coating material applied per minute for any given set of web widths
and web speeds. By inspecting a chart of this nature for any
specific coating operation, the operator may readily adjust the
pumping rate to a required value to obtain the coating weight
desired. It will be understood that for each coating weight
desired, there will be a separate chart to be referred to as
desired. This system of measuring flow rate and web speed lends
itself readily to automation.
In FIG. 14, I have illustrated a method of applying successive
coatings, one over another, using the tension control devices and
coating head of the invention. I have found that by applying a
heated coating of a high viscosity hot melt compound as described,
it becomes possible for a first coating, while still in a partially
set and slightly tacky state, to move over the coating head and
pick up another layer of coating material which is controlled as
before by the web pressure and synchronized pumping speed and web
speed. As a result, I may successively apply different types of
barrier coatings with excellent results.
FIGS. 19 to 23 illustrate a modification of the invention wherein I
have devised a method of differential tensioning. In this method,
variation in linear tension may be induced and localized at two or
more separate sections of a moving web. In carrying out my method
of differential tensioning, the moving web is constantly engaged
between two nip points comprised by a set of pull rolls and a set
of braking rolls. The two sets of rolls are, however, geared
together in a novel manner so that there is induced a predetermined
surface speed differential between the pull rolls and the braking
rolls.
In thus varying tension in two or more separate sections of a
moving web, the braking rolls are comprised by a novel clutch
assembly including two clutch sections both of which sections are
always rotating but at different speeds. Increase in tension with
this arrangement is realized by increasing pressure of one clutch
section against the other, and in a preferred form of my method,
increase in pressure is accomplished by the use of compressed air.
It will be understood that in thus increasing pressure on the
clutch faces, a small slipping factor is present which is reduced
until the clutch faces approach full non-slipping engagement.
An important feature of my method of differential tensioning
resides in the fact that both clutch sections are rotating, and
although rotating at different speeds, the percentage of slip
between the sections is very low, i.e., about 6 to 8 per cent and
therefore the heat dissipation factor is minimal. This is
signficant from the standpoint of paper webs especially since most
paper webs are capable of undergoing from 2 to 3 per cent without
breaking.
In comparison with conventional clutch braking where one clutch
face is stationary and one rotating, the slip factor is very high,
i.e., 96 to 98 per cent, with large power requirements which in
turn necessitate large heat-dissipating capacities. It is pointed
out that with the invention method, there is realized in effect
regenerative braking and, as a practical matter, a constant tension
can be maintained in a web, and especially over a coating head in
an effective and low-cost manner, heretofore not realized in web
tensioning.
One practical application of this tensioning method is to draw off
a web of paper from a supply roll exerting tension from a set of
pull rolls. The web is led through a pair of braking rolls turning
at different speeds, and that portion of the web between the supply
roll and the braking rolls is held at a constant tension. However,
portions of the web moving between the nip of the braking rolls and
the nip of the pull rolls are continuously subjected to a boost in
tension. Other portions of the web leaving the pull rolls and
passing on to a rewinding drum may then be wound at a lowered
tension which may be similar to that exerted by the pull rolls or
some other magnitude.
Considering in further detail the structure shown in FIGS. 19 - 23,
I provide a roll arrangement generally similar to that earlier
disclosed and illustrated in FIGS. 1 and 2. A supply roll E1
mounted on a roll support Y1 furnishes a web W10. A chill roll R10
is rotatably mounted in a frame 2" and in rolling contact therewith
is a roll R11 to provide a first web nip point. Roll R10 is driven
by a motor M10 (FIG. 19) which actuates a pulley M12, a belt M13
and a second pulley M14 on a shaft M15. Fixed to shaft M15 is a
gear M16 which is in mesh with a gear M17 on shaft M18 to which
chill roll R10 is fixed. Rolls R11 and R10 thus constitute a set of
pull rolls for drawing off the web W10 at some desired linear
tension.
Cooperating with the set of pulls comprised by rolls R10 and R11 is
set of rolls R13 and R14 which engage the web W10 to provide a
second nip point and constitute a set of braking rolls.
In accordance with the invention, I provide in the set of braking
rolls noted, a special clutch mechanism. As shown in FIG. 19, the
roll R14, corresponding to the preheat roll R4 earlier described,
is fixed to a shaft M20 and mounted on the shaft M20 is a clutch
mechanism M22. This clutch mechanism includes one side M22a which
is rotatable on shaft M20 and has secured thereto a gear M24, as
shown in FIG. 23. Gear M24 meshes with and is driven by gear M16.
However, the size of gear M24 is chosen such that the surface speed
of roll R14, when driven by gear M16, is less than the surface
speed of roll R10. Clutch M22 is also includes a second side M22b
which is in slipping engagement with the first side and which is
keyed to shaft M20. This fixed clutch section is movable towards
and away from the free clutch by means of a pressure exerted, for
example, by compressed air connected to the clutch at M26, as shown
in FIG. 21, a pressure regulating apparatus such as, for example,
that sold and manufactured by the Watts Regulator Co. of Lawrence,
Mass.
In the drawings, I have illustrated a preferred form of
differential tensioning for dealing with a web of paper to be
coated in the manner earlier described in which the web W10 after
leaving the braking rolls R13 and R14 is passed over a guide roll
R20, a bowed expander roll R21, and then over a coating head T11,
as shown in FIG. 22. From the coating head, the web passes to a
guide roll mechanism F12 and then to the nip point of the pull
rolls R10 and R11.
In handling the paper web described with the clutch mechanism
indicated, I may employ an adjustment such that with the clutch
faces fully engaged in non-slipping relationship, the surface speed
of roll R14 is 10 percent less than the surface speed of roll R10.
Since very few webs to be coated will stretch ten percent before
rupturing or breaking, the clutch must be permitted to slip some
predetermined amount to avoid this. The amount of air pressure on
the clutch determines the amount of tension in the web between the
two nips and remains constant for a given setting. Thus tension
over the coating head remains independent of web tension levels
from the unwinding rolls to the pull rolls and from the pull rolls
to the rewinding rolls. It will be observed that this capability is
essential when it is desired to unwind and/or rewind at tension
levels less than that required for proper coating distribution in
the cross web direction of the coating head.
Another important advantage of this type of clutch operation
resides in conservation of energy resulting from regenerative
braking. Assume one were to apply a conventional brake to roll R14,
one side of the brake would be stationary and the other side
rotating. If, for example, it is desirable to maintain a tension
level over the coating head T11 just short of the braking point of
the web and the ultimate stretch of the web is three per cent, the
tension might be set high enough to remove two per cent with risk
of breaking the web. In such case, with conventional braking and
one side stationary, approximately two per cent of the energy
required is absorbed by the web during stretching and approximately
98 per cent is wasted and must be dissipated by air cooling or
water cooling. This, because higher power requirements are
necessary when higher slip exists, and such higher power energy
must be converted to heat and removed.
In comparison with the invention method, 2 per cent is absorbed by
the web, 8 per cent is lost as slip, and 90 per cent is returned to
the power source. This, due to very low slip, with correspondingly
lower energy loss. It will be apparent that since 90 per cent of
the braking force required is conserved, this same force
represented by power input would necessitate the main power force
being that much larger with conventional braking. Additional
horsepower so required might, for example, exceed other power
requirements by a factor of three or four.
In thus carrying out differential tensioning in the manner
disclosed, I may also desire to combine with the apparatus
described, means for determining and indicating visually, within
rather precise limits, the increase in tension which is being
exerted in the web portions approaching and leaving the coating
head T11. In this connection, I may provide a tension measuring
apparatus which is generally denoted by the reference character TM
and which includes a tension roll and transducer device of a
conventional form such as that manufactured and sold by The Kidder
Press Company of Dover, N.H. This tension roll is mounted in the
frame 2" as indicated diagrammatically in a position to bear
against the web in rolling engagement therewith and change in
tension forces applied to this tension roll are translated by
suitable transducer means and indicated at a dial component TMD
located at some convenient point beside the frame. By means of this
arrangement a machine operator may boost tension on the coating
head while constantly observing the magnitude of the tension
applied and maintaining the tension by means of the air regulator
on the clutch within safe limits as determined by the web strength
present.
* * * * *