[0001] This invention relates to a method and apparatus for decurling web material, particularly
a web of coated or uncoated paper.
[0002] When a web is unrolled, the unrolled web frequently has a tendency to curl. The extent
of this depends ou factors such as the length of time the roll has been stored in
stock and the previous position in the roll of the part of the unrolled web in question
(it will be appreciated that the curvature of the different convolutions making up
the roll differs). In order to compensate for these factors, it has been found desirable
to treat the web to reduce its tendency to curl when unrolled, particularly if it
is ultimately to be cut into sheets. It will be appreciated that the handling, appearance
and convenience of use of such sheets will be facilitated if the undesirable curling
effect is eliminated. Proposals for decurling treatment may be found, for example,
in US Patents 3185616 and 3649447. While such proposals have been found useful, they
have not been altogether satisfactory in the sense that they are expensive and/or
require complicated equipment.
[0003] In the case of a paper web, it is known that increasing the moisture content of the
paper will lead to less trouble from curling than paper having a low moisture content.
Thus it is well-known in the paper industry to seek to counteract curling by the application
of moisture to raw paper stock and/or to coated paper stock. In either case the moisture
is normally applied to the surface opposite to that to which the web will otherwise
tend to curl. With respect to a coated web it is known that the web will tend to curl
towards the coated surface, or, in the case of a web coated on both surfaces, to the
surface last coated, and so the moisture is normally applied to the uncoated surface,
or to the first coated surface.
[0004] Several types of apparatus have been proposed for applying moisture to a moving web.
Examples include roll applicators such as so-called Dahlgren-type systems, electrostatic
systems such as disclosed in US Patent 3467541 and steam applicator systems. The last-mentioned
include firstly systems incorporating a heat conducting backing body to facilitate
condensation of the steam, whereby an increased moisture content may be obtained,
as disclosed in US Patent 2370811 and secondly, systems in which a humid atmosphere
is directed towards the web, as disclosed in US Patent 3238635.
[0005] While these and other techniques have been found useful in applying moisture to a
paper web so as to minimise the undesirable curling properties.of the paper, they
have not proved entirely satisfactory. Electrostatic systems tend to suffer from nozzle
clogging, arcing and misting, and to apply moisture unevenly. Moreover, the need to
take special ; safety precautions is a disadvantage. So far as non-electrostatic systems
are concerned, mere direction of a humid atmosphere towards the web has been found
to be inefficient so far as decurling is concerned. If direct steam showers are employed,
the decurling effect is governed by the steam pressure employed at the shower source.
In order to obtain effective decurling, excessive steam pressures and/or reduced machine
speeds may be necessary. It should be appreciated in this context that steam pressure
affects other important variables such as the web temperature, web to shower distance
and steam billowing. In addition, decurling regulated by steam pressure alone is uneconomical
and inefficient. If the web is free floating, the distance between the web and the
shower source tends to increase and steam tends to billow. These effects result in
an increased total amount of steam being used, in order to ensure that the amount
of steam required for bringing abour decurling actually reaches the web. The additional
steam is wasted since it is merely drawn away by exhaust. The provision of extra exhaust
capacity is also expensive.
[0006] It is an object of the present invention to provide a method and apparatus for steam
decurling a web, such as a web of coated or uncoated paper, which will overcome or
at least mitigate the above-mentioned disadvantages.
[0007] Accordingly, the present invention provides in a first aspect a method for decurling
a web by substantially uniform application of moisture thereto, comprising the steps
of subjecting one surface of the web to a steam shower as the web passes through a
steam treatment station, characterized in that a substantially constant distance is
maintained between the web and the source of the steam shower by directing a gas flow
obliquely towards the web from a gas source disposed adjacent the opposite surface
of the web path from the steam shower, in a manner such that the gas flow is substantially
parallel to the web after the gas flow has impinged on the web.
[0008] In a second aspect, the present invention provides apparatus for decurling a web
by substantially uniform application of moisture thereto, comprising means for passing
the web through a steam treatment station and a steam source for providing a steam
shower to one surface of the web, characterized in that gas flow directing means are
provided on the opposite surface of the web path from the steam source, whereby a
substantially constant distance is maintained in use between the web and the steam
source as a result of impingement of the gas flow on the web and subsequent flow of
gas parallel to the web.
[0009] The gas flow is conveniently a flow of air, and the gas flow directing means is preferably
an air foil assembly.
[0010] The present method and apparatus are particularly suited to the decurling of paper
webs, either coated or uncoated. In the case of a coated web, the steam shower is
normally directed at the uncoated surface of the web, or, if both web surfaces are
coated, at the surface opposite the last-coated surface.
[0011] Normally, the web path is horizontal and the steam shower is directed at the web
from beneath the web.
[0012] The air foil assembly is preferably offset with respect to the source of the steam
shower so as to be just prior thereto in the direction of web movement. This minimises
the possibility of damage to the web material at high or excessive steam pressures.
[0013] The leading surface of the air foil assembly is preferable approximately 0.0125m
to 0.0190m (
1/
2 to
3/
4 inch) prior to the steam source, as viewed in the direction of web travel. The vertical
displacement of the web material from the steam source is preferably approximately
half that from the air foil assembly to the steam source. This may be achieved by
suitable balancing of the air pressure and the steam shower pressure. The preferred
air pressure in the air foil assembly is 178-229 kPa (7-9 inches of water). The preferred
steam shower pressure is approximately 34.5kPa (5 psi), although this is not critical.
Steam pressure above about 206.8kPa (30 psi) should however preferably be avoided.
[0014] Preferably, a plurality of steam shower sources are provided with a corresponding
number of gas flow directing means.
[0015] The or each steam shower source may be a steam pipe with at least one steam emitting
orifice, which is or are normally located along the centre line of the pipe. Such
a steam shower source permits the pressure of steam emitted to be varied, so as to
facilitate uniform application of moisture to the web being treated. The or each steam
shower is preferably located below the web, adjacent to the web surface.
[0016] The invention stems from the finding that the factors most significant in controlling
the curling effect, particularly in relation to paper webs and more especially to
coated paper webs, are the distance between the web and the source of the steam shower,
the web temperature, the steam pressure and the exhaust level. The present invention
permits an efficient regulation of these factors and provides for reliable control
of the distance between the web and the source of the steam shower.
[0017] This minimises any web fluttering effect which might otherwise result from excessive
steam pressures and results in more uniform steam application and penetration of the
web. By controlling the distance between the web and the steam source, billowing is
minimised and the necessity for extreme exhaust conditions is eliminated. The invention
also permits the use of steam pressures less than would be needed with a comparable
conventional method and apparatus.
[0018] It will be appreciated that in the present method and apparatus, there is no need
to make use of an electrostatic field for guiding the moisture to be applied to the
web, and that this is a significant benefit.
[0019] It will also be appreciated that the use of one or more air foil assemblies has the
advantage of permitting a constant distance to be maintained between the web and the
steam source without the need for contact with the web surface. This reduces the possibility
of the surface of the web being impaired or blemished, which is particularly significant
where a coated surface is involved, especially if it is a relatively recently coated
surface. Use of an air foil assembly also provides a cushioning effect on the web
surface in the area immediately above the steam pipe orifice(s). There is also a cooling
effect on the web surface since the air film promotes temperature reduction, thus
causing more efficient steam condensation. Also, when an air foil assembly is used,
it is not usually necessary, as it is with conventional steam decurling apparatus,
to increase the steam pressure when the speed of the web has been increased in order
to achieve the desired decurling effect.
[0020] In order to enable the present invention to be more readily understood, reference
will now be made to the drawings, which illustrate diagrammatically and by way of
example some embodiments thereof and of a conventional apparatus, and of which :-
Fig. 1 is a schematic side view of a conventional steam shower decurling apparatus;
and
Fig. 2 is a schematic side view of an embodiment of steam shower decurling apparatus
according to the present invention.
[0021] Referring first to Fig. 1, a steam shower decurling apparatus generally indicated
1 comprises a steam shower housing 2 containing two steam pipes 3,4 having respective
orifices 5,6. The steam shower housing 2 includes exhaust chambers 10.
[0022] When in use, a web 7 is unwound from a feed roll 8, is passed over the steam pipes
3,4 and is taken up on an idle roll 8. Steam showers issue from the orifices 5,6 of
the steam pipes 3,4 and impinge on the web 7 as it passes over them. Any excess steam
is removed via the exhaust chambers 10.
[0023] In this conventional steam decurling apparatus, the decurling effect is regulated
by steam pressure only and there are no means for maintaining a substantially constant
distance between the web and the steam sources. The steam pressure employed affects
this distance and if it becomes too large as a result of a high steam pressure, excessive
steam billowing may result. To counter this, exhaust levels have to be increased,
but this leads to excessive removal of steam and thus to an increase in steam usage.
[0024] Referring now to Fig. 2, a steam shower decurling apparatus generally indicated 20
comprises a steam shower housing 21 containing two steam pipes 22,23 having respective
orifices 24,25. These orifices are disposed along the centre line of their respective
pipes 22,23. The steam shower housing 21 includes exhaust chambers 29 for controlled
venting of billowing steam from the steam pipes 22,23.
[0025] Two air foil assemblies generally indicated 31,32 are positioned above the respective
steam pipes 22,23 so as to be on the opposite surface of the web path from the steam
pipes. Each air foil assembly comprises an air foil housing 33,34 and an air supply
duct35,36. The ducts 35,36 are attached to a remote air blower (not. shown). Each
air foil housing has an outlet 37 arranged so as to direct air obliquely towards the
web, with the result that the air flow is parallel to the web.
[0026] The use of air foil assemblies of this kind gives rise to a Venturi effect (as witnessed
at the surface of an aeroplane wing). The air emitted through the outlet 37 establishes
a uniform air flow or film pattern directed parallel to the web surface and this prevents
contact of the web with the air foil assemblies whilst at the same time maintaining
the web at a constant distance from the air foil assemblies, and thus also from the
steam shower assemblies.
[0027] Each air foil assembly 33,34 has its leading edge positioned or offset so as to be
just before the orifice 24,25 or centre line of its respective steam pipe 22,23 as
viewed in the direction of web movement. The extent of the offset is indicated as
ℓ and is approximately 0.0125m to 0.0190m (
1/2 to
3/
4 inch). The vertical displacement between each air foil assembly and its respective
steam pipe is indicated asot.
[0028] When in use, a web 26 is unwound from a feed roll 27, is passed between the air foil
assemblies 33,34 and the steam pipes 22,23 and is taken up on an idle roll 28. The
air foil pressure is maintained such that the web floats uniformly between the air
foil assemblies 33,34 and the steam pipes 22,23, with the result that the distance
between the steam pipe orifices 24,25 and the web material 26 is maintained substantially
constant at a value approximately half the vertical displacement α between each air
foil assembly and its respective steam pipe.
[0029] The offset of the air foil assemblies 33,34 with respect to the steam pipes 22,23
minimises the possibility of damage to the web due to high steam pressures. The use
of air foils provides a cushioning effect on the web in the area immediately above
the steam pipes. The upper surface of the web does not actually contact the air foil
assemblies, which is especially significant when the upper surface of the web carries
a coating, since the possibility of impairing the web surface is reduced.
[0030] The steam pressure employed in the apparatus of Fig. 2 is generally about 34.5kPa
(5 psi) and is preferably not greater than 206.8kPa (30 psi).
[0031] It will be appreciated that the apparatus of Fig. 2 does not utilise electrostatic
means for guiding moisture to be applied to the web.
1. A method for decurling a web by substantially uniform application of moisture thereto,
comprising the step of subjecting one surface of the web to a steam shower as the
web passes through a steam treatment station, characterized in that a substantially
constant distance is maintained between the web and the source of the steam shower
by directing a gas flow obliquely towards the web from a gas source disposed adjacent
the opposite surface of the web from the steam shower, in a manner such that the gas
flow is substantially parallel to the web after the gas flow has impinged on the web.
2. A method as claimed in Claim 1, characterized in that the source of the flow of
gas is offset with respect to the source of the steam shower, so as to be just prior
thereto as viewed in the direction of web movement.
3. A method as claimed in Claim 2, characterized in that the gas flow pressure is
approximately 178 to 229kPa (7-9 inches of water) and the steam shower pressure is
approximately 34.5kPa (5 psi).
4. A method as claimed in any preceding claim, characterized in that a plurality of
steam shower sources and a corresponding number of gas flows are provided.
5. A method as claimed in any preceding claim, characterized in that the web comprises
an optionally coated paper sheet.
6. Apparatus for decurling a web by substantially uniform application of moisture
thereto comprising means for passing the web through a steam treatment station and
a steam source for providing a steam shower to one surface of the web, characterized
in that gas flow directing means are provided adjacent the opposite surface of the
web path from the steam source, whereby a substantially constant distance is maintained
in use between the web and the steam source, as a result of impingement of the gas
flow on the web and subsequent flow of gas parallel to the web.
7. Apparatus as claimed in Claim 6 characterized in that the gas flow directing means
comprises an air foil assembly.
8. Apparatus as claimed in Claim 7, characterized in that the air foil assembly is
offset with respect to the steam source so as to be just prior thereto, as viewed
in the direction of web movement.
9. Apparatus as claimed in Claim 8, characterized in that the extent of the offset
is approximately 0.0125m to 0.0190m (1/2 to 3/4 inch).
10. Apparatus as claimed in any of Claims 6 to 9, characterized in that a plurality
of steam shower sources and a corresponding number of gas flow directing means are
provided.