[0001] The present invention relates to methods of and apparatus for applying or coating
fluid materials, including but not restricted to hot melt type liquids and adhesives
of a wide variety of viscosities, to surfaces (hereinafter generically referred to
as webs), being more particularly directed to such coating with the aid of novel
porous roll surfaces and the like.
[0002] Various types of hot melt and other fluid apparatus and coaters have been heretofore
employed to provide continuous, intermittent and patterned coatings upon web surfaces,
including slot nozzle applicators employed with metered pumped fluid supply systems,
as described in my earlier U.S. Patents Nos. 3,595,204, and 4,277,301, and commutating
cylindrical apparatus as in U.S. Patent No. 3,294,060.
[0003] Underlying the present invention, however, is the discovery that great flexibility
in coating can be obtained through metering the fluid through a porous cylindrical
shell or roll, enabling both ready direct and indirect or transfer coating of one
or multiple hot melt or room temperature fluids, including hot melts of high viscosity,
and with reduced pressure drops over prior art techniques, and in continuous, intermittent
or patterned coatings at will.
[0004] An object of the present invention is to employ the features of this discovery to
provide, accordingly, a novel method of and apparatus for fluid application that enables
such and other improved operation through the use of porous roll fluid-metering coating.
[0005] A further object is to provide such a new and improved coating applicator that enables,
also, simultaneous pattern coatings and stripes of different fluid coat weights;
continuous, pattern and stripe simultaneous coatings of dissimilar fluid coating
materials; and successive and superimposed fluid coatings.
[0006] Other and further objects will be explained hereinafter, such being more particularly
delineated in the appended claims.
[0007] In summary, from one of its broad viewpoints, the invention embraces a method of
coating a web with fluid material, that comprises, pumping such fluid material with
one of continuous and intermittent metered flow along a predetermined longitudinal
path, exiting the same at a region transverse thereto, receiving the transversely
exited fluid in a reservoir volume extending along and enveloping said path, exiting
the fluid from said reservoir volume through a porous surface co-extensive with and
bounding said reservoir volume, relatively rotating the said porous surface and the
said region of fluid exiting from said path, and applying the fluid longitudinally
exited through the porous surface to said web while moving the web transversely past
the same to coat the web with the fluid as metered through the pores of the porous
surface. In apparatus form, the invention contemplates fluid coating apparatus having,
in combination, means for continuously or intermittently pumping the coating fluid
along a longitudinally extending conduit terminating in an opening adjusted for transversely
exiting the fluid, a cylindrical annular reservoir volume enveloping the conduit
and its opening for receiving the exited fluid, a cylindrical porous shell externally
bounding the cylindrical reservoir to constitute a fluid dispensing roll, means for
relatively rotating the conduit and its fluid exiting opening and the roll to cylindrically
distribute the exited fluid along the reservoir volume, and means for rotating said
roll and applying the fluid dispensed through the porous shell to web means drawn
transversely past the roll. Preferred and best mode embodiments and modifications
are hereinafter detailed.
[0008] The invention will now be described with reference to the accompanying drawings,
Figs. 1A and B of which are isometric (exploded) and transverse sectional views of
a novel porous roll applicator designed for use in accordance with the present invention;
Fig. 2 is a view similar to Fig. 1A of a modified multiple section porous roll applicator;
Figs. 3A and 3B are transverse fragmentary sections, upon an enlarged scale, of standard
and differential porosity (micron) weight porous shells for the applicator;
Figs. 4A and 4B show, respectively, illustrative single and multiple width repeat
coating patterns attainable with apparatus of the type shown in Figs. 1A and 2;
Figs. 5A, 5B and 5C are schematic side elevations of typical applicator configurations
useful with the invention for transfer, direct and differential or different material
coatings, respectively;
Fig. 6 is a more detailed system diagram for such transfer and/or direct coating,
suitable for both continuous full coating (Fig. 7A) and patterns such as continuous
longitudinal stripes with intermittent transverse stripes (Fig. 7B).
Fig. 8 is a system diagram similar to Fig. 6 of a multiple supply, differential or
different material coating system suitable for pattern coatings or intermittent,
differential stripe and/or continuous stripe coatings (Fig. 9); and
Fig. 10 is a similar system diagram for a modified multiple supply system suitable
for full coating of two different materials, such as one over another (Fig. 11).
[0009] Referring to Figs. 1A and 1B, a preferred porous roll applicator construction is
illustrated for continuously or intermittently pumping the coating fluid from a single
supply port at a rotary joint union 2 along a longitudinally extending conduit 2ʹ
terminating in a transversely radially extending opening 2ʺ within a cylindrical
inner supply conduit 4 -- the inlet 2ʹ extending preferably axially along the roll
4 and the opening 2ʺ exiting fluid transversely therefrom. A coaxial cylindrical
annular reservoir cavity or volume 6 envelops the inner roll conduit 4 and receives
the exited fluid at 2ʺ. The reservoir volume 4 is coaxially externally bounded by
a cylindrical porous shell 8, as of sintered metal, screening or the like, as later
more fully described, with the conduit 4 and its fluid exiting opening 2ʺ being relatively
rotatable to distribute the fluid within and along the reservoir to keep the same
filled and applying fluid uniformly longitudinally along the porous shell 8. The
porous shell may, for example, be of uniform sintered metal construction, say 20 micron
pores, as in Fig. 3A, or may employ multiple varying or different porosity (and weight)
shells as in Fig. 3B, such as a 10 micron outer shell occupying, say, 10% of the total
shell thickness, and a 100 micron inner concentrate shell portion of 100 microns,
constituting the balance of the shell thickness. The differential micron construction
will reduce the pressure drop for high viscosity materials such as 10,000-30,000
cps at room temperature, when metered through the porous metal shell. The outer surface
of the porous shell roll 8 may be varied not only in degree of porosity, but also
in surface preparation or extent, as at 8ʹ in Fig. 1A, to introduce predetermined
patterns in the coating, such as the repeat coating horizontal stripes or longitudinal
side stripes and intermittent horizontal stripes of Fig. 4A. The patterns may be metered
into the surface of the roll by special etching after the surface pores have been
machined closed.
[0010] While porous sintered metal cylinders have heretofore been used for the very different
applications of air film as bearing rolls, wicks and filter cartridges and the like,
suitable sintered stainless steel, Monel and similar porosities of 10, 20 or 40 microns
in shell thickness of the order of 3/8 inch have been successfully employed for this
very different usage as a viscous fluid metering coating roll. Among such are the
Series 1400 of Mott Metallurgical Corporation of Farmington, Connecticut. This unique
usage is more clearly delineated in Figs. 5A and 5B, showing the porous apparatus
roll 8 used for transfer and direct coating to moving webs, respectively. In Fig.
5A, the porous roll 8 is rotated in contact with a rubber-coated steel mandrel or
similar applicating roll 10 that transfers the coating fluid from the porous dispensing
roll 8 to the web (so-labelled) as it moves between the roll 10 and the lower laminating
roll 12, rotating oppositely to the roll 10. The laminating roll insures positive
web contact against the applicating roll for fluid transfer. The porous roll 8 rotates
oppositely to the transfer or applicating roll 10 and preferably either with the same
surface speed thereof or synchronously therewith, or proportional thereto (including
fractional speed). The applicating roll operates at web speed or at a slightly less
speed to create a smeared surface. Typical speed can be as low as 95% of web speed.
In Fig. 5B, on the other hand, the porous roll 8 itself directly contacts the web
as the same moves between the roll 8 and an oppositely rotating lower laminating roll
12 which insures positive contact of the web with the porous roll. In such direct
coating usage, the porous roll 8 runs synchronous to the web speed for pattern print
coating; or at a slightly less speed for full width coating or continuous stripes
(longitudinal in web direction) to create a smeared surface. The systems of Figs.
5A and 5B permit full, or continuous, stripe and pattern coatings in single weight
coats.
[0011] A more complete system for that schematically shown in Figs. 5A is shown in Fig.
6 applied to the illustrative example of hot melt adhesives as of the types described
in said patents or other well-known coatings of this type, fed from a hopper 1 through
a filter 3 to a positive displacement metering pump 5 (such as that of said patents)
to supply fluid at 7 to a three-way valve 9 (as, for example, of the type described
in my U.S. Patent 4,565,217) that supplies the rotary union inlet 2 of the porous
roll system 8. A return feed back to the filter input is shown at 11. The metering
pump 5 is controlled by a digital pump drive 13 which is connected to a web reference
magnetic pick up sensor 15 contacting the web to synchronize the pump speed with
the web speed. Examples of full or continuous coatings and continuous longitudinal
stripe and intermittent horizontal stripe patterns are shown in Figs. 7A and 7B.
[0012] Multiple width porous roll applicators may also be provided as shown in Fig. 2, illustrating
multiple inlet supply ports and rotary union 2, multiple width successive inner supply
rolls 4, with successive section separators 4ʹ between adjacent rolls separating the
respective successive reservoir cavities and porous roll shell sections. Fig. 4B
illustrates typical exemplary multiple width repeat coating patterns.
[0013] Turning to the before-mentioned flexibility of the invention to enable stripe or
other pattern coatings of different coat weights simultaneously or full, stripe or
pattern coatings of dissimilar fluid coating materials simultaneously, reference is
made to the schematic application modification of Fig. 5C, dealing with such differential
or different material coatings. This design would permit stripes or pattern coatings
of different coat weights simultaneously. The combination of two porous rolls permits
applying layer upon layer of two identical or dissimilar fluids side by side, or the
same fluid applied at different coat weights, to meet a specific customer coating
pattern. In Fig. 5C, the porous roll 8 (with a pattern #1, for example) is shown contacting
one upper side portion of the oppositely rotating applicator roll 10 between which
and the laminating roll 12, the web is moved. A second porous roll 8ʹ (pattern #2
or different coating weight or material, for example) simultaneously contacts the
opposite side of the applicator roll 10. The porous rolls 8 and 8ʹ can run synchronously
with or at fractional differential speed to the applicating roll 10 which, in turn,
may, if desired, run at a fractional differential speed to that of the web.
[0014] A complete system for such different material or differential operation is shown
in Fig. 8, wherein the second porous roll 8ʹ is shown fed from a second positive displacement
metering pump 5ʹ, feeding at 7ʹ a second 3-way valve 9ʹ for inputting the second
porous roll assembly 8ʹ, and with a return line 11ʹ to the input of the filter 3.
The pump 5 feeding the porous roll 8 is shown as a dual discharge metering pump with
supply lines 7 and 7A. Fig. 9 illustrates an exemplary pattern coating of intermittent
differential weight stripe (supply line 7ʹ -- say, 2 mol coating) and continuous longitudinal
side stripes (supply lines 7 and 7A -- say, 1 mil coating).
[0015] As previously noted, the flexibility of the invention also extends to multiple coatings
of two different fluid coating materials, one over the other as in Fig. 11. The system
of Fig. 10 enables this with a structure similar to that of Fig. 8, but involving
separate material hoppers 1 and 1ʹ and pumps 5 and 5ʹ, as shown for the different
fluid materials.
[0016] The porous roll applicating technique of the invention is useful with room-temperature
liquids and with hot melt type liquids, at operating temperatures of 350°F, and fluid
coating applications of other temperature ranges. This can be accomplished by installing
heating elements within the porous roll assembly, or using the porous metal material
8 as an electrical conductor/resistor, receiving heating current. Typical material
used for resistance heat would be Nichrome metal.
[0017] Industrial applications for hot melt pattern coatings are required, for example,
in the cigarette industry. Typically, the attachment of the filter covering paper,
known as tipping paper, joining the filter element to the cigarette, requires parameter/
rectangular adhesive pattern with the center area open, without adhesive. Present
cigarette making machines are operating up to 7,000 cigarettes per minute, which represents
the drying limita tion of conventional polyvinyl resin adhesive. Any further increase
in line speed prevents succesful adhesive attachment and drying of the cigarette components.
Hot melt coating used with the present invention in place of the resin adhesive permits
a further increase in production speed. The hot melt will be applied at a low coating
thickness, such as 1 mil, in order to obtain satisfactory bond of the cigarette components.
[0018] In addition to coatings previously described, the invention is particularly useful
with room temperature materials such as silicones, polyvinyl acetates and other adhesive
coatings, and with hot melts such as the etholene vinyl package sealing materials.
[0019] Further modifications will also occur to those skilled in the art, and such are considered
to fall within the spirit and scope of the present invention as defined in the appended
claims.
1. A method of coating a web with fluid material, that comprises, pumping such fluid
material with one of continuous and intermittent metered flow along a predetermined
longitudinal path, exiting the same at a region transverse thereto, receiving the
transversely exited fluid in a reservoir volume extending along and enveloping said
path, exiting the fluid from said reservoir volume through a porous surface co-extensive
with and bounding said reservoir volume, relatively rotating the said porous surface
and the said region of fluid exiting from said path, and applying the fluid longitudinally
exited through the porous surface to said web while moving the web transversely past
the same to coat the web with the fluid as metered through the pores of the porous
surface.
2. A method as claimed in claim 1 and in which said reservoir volume and its bounding
porous surface are coaxially cylindrically shaped transversely of the web, said volume
being annular and said porous surface comprising a cylindrical roll.
3. A method as claimed in claim 2 and in which said applying is effected by contacting
the moving web with the porous surface roll while rotating the roll.
4. A method as claimed in claim 3 and in which said web is moved between oppositely
rotating porous surface and laminating rolls.
5. A method as claimed in claim 2 and in which said applying is effected by contacting
said porous surface roll with an oppositely rotating applicating roll that contacts
the web and transfers the fluid exiting said pores and carried by said applicating
roll to the web.
6. A method as claimed in claim 3 and in which said porous surface roll is rotating
at a speed substantially synchronous with the web speed or proportional thereto.
7. A method as claimed in claim 5 and in which said porous surface and applicating
rolls are rotated at substantially synchronous speed or proportional thereto.
8. A method as claimed in claim 5 and in which the porous surface roll and applicating
roll and rela tively rotated to run at one of substantially synchronous and fractional
differential speeds, and said applicating roll is rotated to run at one of substantially
synchronous and fractional differential speeds relative to the web speed.
9. A method as claimed in claim 5 adapted for multiple coatings and in which a second
fluid ejecting porous surface roll is simultaneously rotated in contact with the applicating
roll at a different point of contact than the first-named porous surface roll to coat
the web with the second fluid.
10. A method as claimed in claim 9 and in which the second porous surface roll is
rotated to run at one of substantially synchronous and fractional differential speeds
relative to the applicating roll.
11. A method as claimed in claim 5 and in which a second fluid ejecting porous surface
roll is employed substantially simultaneously to coat the web with the second fluid.
12. A method as claimed in claim 1 and in which the porosity of said porous surface
varies in at least one of surface extent and degree of porosity in accordance with
a predetermined pattern to provide a patterned coating.
13. A method as claimed in claim 12 and in which said porosity is provided at spaced
portions only of said porous surface to provide spaced stripe coatings.
14. A method as claimed in claim 11 and in which the porosity pattern on the porous
roll surfaces is varied in at least one of surface extent and degree to produce different
coating pattern portions along the web from the first and second fluids.
15. A method as claimed in claim 14 and in which at least one of said porous surfaces
is patterned with porous sections to produce at least one of longitudinal and transverse
spaced coating stripes. A method as claimed in claim 1 and in which said porous surface
is heated to enable the dispensing of hot melt fluids and the like from a source of
the same feeding along said path.
17. A method as claimed in claim 16 and in which said porous surface is of electrically
conducting material and the heating is effected by passing electrical current therealong.
18. A method as claimed in claim 17 and in which the porous surface temperature is
monitored and the current is controlled in accordance therewith.
19. A method as claimed in claim 1 and in which the further steps are performed of
providing a plurality of fluid paths for pumped fluid each transversely exiting its
fluid at successively longitudinal regions, dividing the reservoir volume into a corresponding
plurality of successive longitudinal sections each having its enveloping porous surface
and each sealed from one another, one corresponding to and receiving fluid from its
corresponding fluid path.
20. A method as claimed in claim 11 and in which the fluids are selected and the rotation
speeds of said rolls are adjusted to produce at least one of simultaneous pattern
coatings and stripes of different fluid coat weights; continuous, pattern and stripe
simultaneous coatings of dissimilar fluid coating materials; and successive and superimposed
fluid coatings.
21. Fluid coating apparatus having, in combination, means for continuously or intermittently
pumping the coating fluid along a longitudinally extending conduit terminating in
an opening adjusted for transversely exiting the fluid, a cylindrical annular reservoir
volume enveloping the conduit and its opening for receiving the exited fluid, a cylindrical
porous shell externally bounding the cylindrical reservoir to constitute a fluid dispensing
roll, means for relatively rotating the conduit and its fluid exiting opening and
the roll to cylindrically distribute the exited fluid along the reservoir volume,
and means for rotating said roll and applying the fluid dispensed through the porous
shell to web means drawn transversely past the roll.
22. Apparatus as claimed in claim 21 and in which the applying means comprises means
for directly contacting the porous shell of the roll with one surface of the web
at a region where a cooperative roll engages the opposite surface, to fluid coat the
said one surface of the web.
23. Apparatus as claimed in claim 21 and in which the applying means comprises applicator
roll means contacting the porous shell roll and rotating oppositely to the rotation
of the same, the applicator roll means contacting one surface of the web at a region
where a cooperative roll engages the opposite surface, to transfer the fluid dispensed
through the porous shell to coat said one surface of the web.
24. Apparatus as claimed in claim 23 and in which a further fluid-dispensing porous
shell roll is provided contacting the applicator roll means at a different location
from contact with the first-named porous shell roll and simultaneously therewith to
provide a further fluid coating on the web.
25. Apparatus as claimed in claim 21 and in which the porous shell is patterned to
provide one of spaced porous sections and variations in dimensional extent and degree
of porosity.
26. Apparatus as claimed in claim 21 and in which a plurality of longitudinally extending
coating fluid conduit means is provided each transversely exiting fluid at successive
longitudinal regions into corresponding successive enveloping cylindrical annular
reservoir sections having corresponding porous shells, and means being provided for
sealing each section from the adjacent section.
27. Apparatus as claimed in claim 21 and in which the porous shell is constructed
of one of sintered metal and screening.
28. Apparatus as claimed in claim 23 and in which the fluid and roll rotation rates
are selected to produce on the web at least one of simultaneous pattern coatings
and stripes of different fluid coat weights; continuous, pattern and stripe simultaneous
coatings of dissimilar fluid coating materials; and successive and superimposed fluid
coatings.