Field of the invention
[0001] The invention relates to an arrangement for producing coated board as defined in
the preamble of the independent claim 1.
[0002] The invention also relates to a method for producing coated board as defined in the
preamble of the independent claim 12.
[0003] A traditional way of drying a coating of a board produced in a separate or on-line
board machine is using a combination of an infrared (IR) dryer, an air dryer and a
cylinder dryer. IR dryer has an advantage of being small in size so that it fits well
near to a blade coater, which is a typical coater for coating boards. IR dryer is
typically used for pre-heating and initial drying of wet coatings before a board comes
into contact with cylinders which finishes the drying of a coating of a board. Normally
IR dryers are installed as the first dryers after a coating station to increase the
web temperature to the level where fast dewatering makes quick consolidation of the
coating color possible.
[0004] EP 1 379 731 B1 discloses an arrangement in the manufacture of coated printing paper based on doctor
blade coating technique. It discloses that a paste-like substance is applied on the
surface of the printing paper on a coating station and after the coating station the
paper passes into a dryer which comprises an infrared dryer and an air dryer and finally
the paper web continues to a cylinder group in which the drying of the coated paper
continues.
[0005] WO 2008/034513 A1 discloses a method in an online machine for producing coated paper or paperboard.
In the method web is formed from a fibrous material mixture in a wire section, the
web is dewatered in a pressing section and dried in a drying section which comprises
drying cylinders. A precoating is applied to both web sides by way of a size or film
press and dried with contactless dryers and in an afterdrying section comprising drying
cylinders. The web is presmoothed by way of a soft nip or hard nip calender and finally
reeled. A pigment-containing application medium is applied to only one web side of
the web after the presmoothing, for which purpose a first coating device, for example
a film coater, is used for applying the application medium indirectly by means of
an applicator roll and/or a second coating device, for example a blade coater, is
used for applying the application medium directly.
[0006] Problem with the above mentioned prior art is that the layout of the machine becomes
complicated and the drying of the board is not energy efficient enough for today's
energy requirements.
Objective of the invention
[0007] The object of the invention is to provide an energy efficient drying of a coating
of a board in a board machine comprising an online coating station followed by a drying
section.
Short description of the invention
[0008] The arrangement for producing coated board according to the invention is characterized
by the definitions of the independent claim 1.
[0009] Preferred embodiments of the arrangement are defined in the dependent claims 2 to
11.
[0010] The method for producing coated board according to the invention is correspondingly
characterized by the definitions of independent claim 12.
[0011] Preferred embodiments of the method are defined in the dependent claims 13 to 14.
[0012] The invention relates to an arrangement for producing coated board, the arrangement
comprising a board machine for producing board and a coating station for applying
coating on the surface of the board.
[0013] In a preferred embodiment of the invention board produced in a board machine is coated
online in a coating station, preferably in a blade coater, and after that the coating
of the board is dried in a drying section solely by means of air. In other words the
coating station is arranged online to the board machine and the arrangement further
comprises a drying section comprising a contactless air dryer, said drying section
arranged after the coating station in a machine direction for drying the coating of
the surface of the board, said coating is solely dried by means of air drying. The
drying section comprises an air dryer such as an impingement dryer. An impingement
dryer is used especially when board is coated only on one side. The single-sided impingement
hood is arranged on the side to which the coating is applied and the board is then
supported on the opposite side with supporting rolls. The supporting rolls can be
arranged to form a linear or curved bath under the dryer. The impingement temperature
of air dryer can be on a level of 250 - 450 °C. Although an impingement dryer is typically
used when coated only on one side, it can also be used when both sides are coated
i.e. it can be used for double sided air drying. The coating station is a blade coater,
a curtain coater, a film coater or an air brush coater.
[0014] The invention relates also to a method for producing coated board, said method comprising
a step of producing board in a board machine, a step of applying coating on the surface
of said board in a coating station and a step of drying said coating in a drying section.
The coating station is arranged online to the board machine and the coating is solely
dried by means of air drying in the drying section. The coating is dried by at least
one air dryer arranged in the drying section and the coating is applied on the surface
of the board by a blade coater, a curtain coater, a film coater or an air brush coater.
[0015] In the drying section the coating of the board is solely dried by air such that the
drying section can comprise multiple air dryers. Typically the drying section comprises
two or three air dryers arranged after the coating station. The board can be coated
on both sides in which case a second coating station with a second drying section
follows the first drying section. In between the first drying section and the second
coating station a drawing roll group, a cylinder group or a drawing nip is preferably
but not necessarily arranged to help the tail threading of the board or can used for
controlling the tension of the board but they do not have any drying properties. The
cylinder group can be a cooling cylinder group which cools the board such that the
board is not too hot when arriving to a next coating station. In other words a cooling
cylinder group reduces absorption of water from the coating. Means for controlling
tension of the board is arranged after the drying section and are used for controlling
tension of the board or for tail threading purposes, but not for drying of the board.
Means for controlling tension of the board is preferably a drawing roll group or a
drawing roll nip, but other suitable means for controlling tension of the board can
also be used, such as a cooling cylinder group for cooling the board at the same time
when used for controlling tension of the board or an S-wrap. S-wrap is achieved by
arranging cylinders such that the board travels an S-shaped path. The means for controlling
tension of the board do not need to be arranged after every coating and/or drying
station, another option is to arrange them after every second station as well. Finally
the board is reeled.
[0016] Another possible embodiment of the invention is to use an air flotation dryer in
the drying section after the board is coated. Air flotation dryer is used especially
when the board is coated on both sides simultaneously or when one side of the board
is coated and the other side is for example surface sized or moistened. In an air
flotation dryer a board is supported on both sides by air jets or air cushions. One-sided
air floatation dryers can also be used. Nozzles used in air flotation dryers are preferably
arranged to have a distance of less than 20 mm to the board surface.
[0017] The drying section according to this invention comprises only contactless air dryers
such that the coating of the board is solely dried by air. The air contactless air
dryers are either impingement dryers, air flotation dryers or a combination of these.
An air dryer, such as an air flotation dryer or an impingement dryer, is heated with
in-line gas burner or steam coils. Make-up air and combustion air can be taken directly
from a fan room or they can be preheated in a heat exchanger. So the heat exchanger
is arranged to preheat air used in the gas burner. The energy efficiency of gas heated
air dryers can be increased by using heat exchangers where the exhaust air heats up
the burner air and make up air and by using the exhaust air in steam heated air dryers.
The impingement air is preferably circulated back to the dryer in order to maintain
good energy economy. The impingement air can be recirculated by a fan, heated by gas
burners and then distributed back to dry the coating of the board. By arranging a
heat exchanger and circulating air coming from gas heated burners to steam coils,
an efficiency rate of about 85% can be achieved. A heat exchanger can also be arranged
for exhaust air coming from air flotation dryers.
[0018] The air dryers can be used for moisture profiling in a cross machine direction to
prevent non-uniform board properties. In other words a contactless air dryer is arranged
to adjust and/or control the moisture profile of the board in a cross machine direction.
[0019] The advantage of this invention is to have a compact online finishing section and
especially drying section after a coating station in a board machine and having low
energy consumption while drying the coating of the board.
List of figures
[0020] In the following the invention will be described in more detail by referring to figures,
in which
Fig. 1 shows a prior art coating and drying arrangement for board,
Fig. 2 shows one embodiment of the invention, and
Fig. 3 shows another embodiment of the invention.
Detailed description of the invention
[0021] The figure 1 shows an example of a prior art arrangement for drying the coating of
the board. Although not shown in the figure the prior art arrangement is an offline
process which means that after the board is produced in a board machine it is reeled
to be a parent reel and then transferred to an offline coater to be coated in a separate
finishing section.
[0022] In the finishing section the first side of the board is coated first on a first blade
coater 11 and right after the coating is applied to the surface of the board it goes
to a first drying section 21 comprising an IR dryer 21i, two successive air dryers
21a, 21b and a cylinder group 21g. The coating of the board starts drying in an IR
dryer 21i. The IR dryer 21i increases the board temperature to a level where fast
dewatering makes a quick consolidation of coating color possible. After the IR dryer
21i the board passes into a first air dryer 21a. Figure 1 shows two successive air
dryers 21a, 21b. After the two air dryers 21a, 21b the board passes into a cylinder
group 21g for further drying. After the drying section 21, i.e. after these four different
drying devices the board is coated on the other side as well so another coating station
12 is arranged to coat the uncoated side of the board. After the second coating station
12 which is a blade coater as well a second IR dryer 22i is arranged to dry the coating
of the board. The IR dryer 22i is used the same way as the first one, i.e. to start
the drying process efficiently before the board moves to air dryers 22a, 22b. After
the air dryers 22a, 22b the board passes into a cylinder group 22g for the final drying
of the coating of the board. This arrangement produces board that is coated twice
on the upper surface and once for the opposite surface so the board passes after the
cylinder group 22g into a third coating station 13 for applying coating to the surface
of the board. The third coating station 13 and the third drying section 23 repeats
the preceding process in which the board is coated on the blade coater 13 and after
the coating is applied to the surface of the board it passes into an IR dryer 23i
which starts the drying of the coating and after which the board passes into two successive
air dryers 23a, 23b and finally to a cylinder group 23g to finish the drying of the
coating of the board. After the last cylinder group 23g the coated board is reeled
in a reel 50.
[0023] Drying efficiency of an IR dryer, i.e. the part of electrical energy that is consumed
in the heating of the board or evaporation of water, is 25-40%. Some parts of the
halogen lamp and the reflectors used in IR dryers cannot stand high temperatures so
they have to be cooled. There are also gas IR dryers using gas as an energy source.
The portion of energy content of the gas which is transferred to radiation is about
28-55%.
[0024] The main idea of the arrangement for producing coated board according to the invention
is to have more energy efficient drying of a coating of a board and this is achieved
by using only contactless air drying. Air dryers are typically heated with in-line
gas burners or steam coils. Steam pressure in the coils can be regulated so that the
impingement temperature can be controlled. The in-line gas burners have a wide area
for controlling the impingement temperature. A good energy economy is maintained by
circulating about 80-90% of the impingement air back to the dryer and the remaining
air is removed as exhaust air. The arrangement according to the invention can comprise
air dryers that dry the coating of the board on both sides. Both sided drying is useful
when controlling the curling of the board. In prior art arrangements IR dryers are
used also to heat the board itself but when arranging an online finishing section
with air dryers the need to heat the board is not present anymore and all the heating
energy is used for drying the coating of the board.
[0025] The figure 2 shows a first embodiment of the arrangement according to the invention.
For the purposes of clarity the figure 2 shows only the finishing section of the board
machine although the finishing section is arranged online to the board machine without
any reeling or unreeling before it. The board comes from the previous section, which
is normally a drying section, to a first coating station 11. The first coating station
11 is preferably a blade coater in which the coating is applied to the board by means
of an application roll and the final coating is controlled by a metering blade. Other
possibilities for a coating station are a film coater, a curtain coater or an air
brush coater. After the first side of the board is coated in the first coating station
11 the board passes into a first drying section 21 which comprises an air dryer 21a,
21b, 21c preferably in the form of an impingement dryer such that the coating of the
board is solely dried by means of air drying. The impingement dryer is preferable
in the situation where only one side of the board is coated at a time. An air flotation
dryer can be used in situations where both sides of the board are coated simultaneously.
A drying section 21, 22, 23 can comprise more than one air dryer but such that the
coating of the board is solely dried by air. This means that after a coating station
11, 12, 13 the coating of the board is solely dried by means of air drying. In this
embodiment there are three successive air dryers 21a, 21b, 21c arranged to dry the
coating of the first side of the board. After the first drying section 21 the board
passes into a first drawing roll group 31 which is used for controlling the tension
of the board and for tail threading. After the first drawing roll group 31 the board
passes into a second coating station 12 into which the uncoated side of the board
is coated. From the second coating station 12 the board passes into a second drying
section 22 comprising three air dryers 22a, 22b, 22c for drying the coating of the
board solely by means of air. After the second drying section 22, in which the coating
of the board has dried in three air dryers 22a, 22b, 22c, it travels to the next drawing
roll group 32. This embodiment shows an arrangement for producing coated board that
comprises two coating layers on one side of the board and one coating layer on the
other side of the board. For this reason the board travels after the second drawing
roll group 32 into a third coating station 13. In this third coating station 13 a
second coating layer is applied to the first side of the board which was coated in
the first coating station 11. After the third coating station 13 the board passes
into a third drying section 23 comprising three air dryers 23a, 23b, 23c after which
the board passes into a third drawing roll group 33 and finally to the reeling section
50 to be reeled.
[0026] The figure 3 shows another embodiment of the invention in which the board path goes
the same way as in figure 2 and the online process, i.e. the finishing section being
in an online connection to the board machine, comprises three coating stations 11,
12, 13 in which the surface of the board is coated and after each coating station
11, 12, 13 the coating of the board is dried in a drying section 21, 22, 23 in which
there are three successive air dryers to dry the coating of the board solely by means
of air. All three air dryers in each drying section 21, 22, 23 dry the coating of
the board solely by means of air such that after the board has left the last dryer
of the coating section the coating of the board is dry enough so that it will not
be damaged when moving forward to a next phase in the finishing section. In this embodiment
the first dryer 21a in the first drying section 21 is an air flotation dryer having
air temperature of over 400 °C or even over 450 °C.
[0027] The coating station 11, 12, 13 is preferably a blade coater, but it can be a curtain
coater, a film coater or an air brush coater as well. The board tension is controlled
by a drawing roll nip 31, 32, 33 arranged after each drying section 21, 22, 22. In
figure 2 the arrangement comprised a drawing roll group instead of a drawing nip which
the drawing roll group takes more space compared to this embodiment with a drawing
roll nip and when space for finishing section is limited the drawing nip can be more
advantageous. Finally after the last drawing roll nip 33 the board passes into a reeling
section with a reel 50.
[0028] In figures 2 and 3 any one of the coating station can be replaced by a surface sizing
station for surface sizing one or both sides of the board or moisturizing station
for moisturizing one or both sides of the board.
[0029] It is apparent to a person skilled in the art that as technology advanced, the basic
idea of the invention can be implemented in various ways. The invention and its embodiments
are therefore not restricted to the above examples, but they may vary within the scope
of the claims.
1. An arrangement for producing coated board, the arrangement comprising
a board machine for producing board, and
a coating station (11, 12, 13) for applying coating on the surface of the board,
characterized
in that the coating station (11, 12, 13) is arranged online to the board machine, and
in that the arrangement further comprises a drying section (21, 22, 23) comprising a contactless
air dryer (21a, 21b, 21c, 22a, 22b, 22c, 23a, 23b, 23c), said drying section (21,
22, 23) is arranged after the coating station (11, 12, 13) in a machine direction
for drying the coating on the surface of the board, said coating is solely dried by
means of air drying.
2. The arrangement according to claim 1, characterized in that the arrangement further comprises means (31, 32, 33) for controlling tension of the
board, said means (31, 32, 33) for controlling tension of the board is arranged after
a drying section (21, 22, 23) in a machine direction.
3. The arrangement according to claim 2, characterized in that the means (31, 32, 33) for controlling tension of the board is a drawing roll nip
or a drawing roll group.
4. The arrangement according to claim 2, characterized in that the means (31, 32, 33) for controlling tension of the board is an s-wrap.
5. The arrangement according to claim 2, characterized in that the means (31, 32, 33) for controlling tension of the board is a cooling cylinder
group for cooling the board.
6. The arrangement according to any preceding claims, characterized in that the contactless air dryer (21a, 21b, 21c, 22a, 22b, 22c, 23a, 23b, 23c) is an air
floatation dryer or an impingement dryer or a combination of these.
7. The arrangement according to claim 6, characterized in that the contactless air dryer (21a, 21b, 21c, 22a, 22b, 22c, 23a, 23b, 23c) is arranged
to adjust and/or control the moisture profile of the board in a cross machine direction.
8. The arrangement according to claim 6 or 7, characterized in that the air floatation dryer or the impingement dryer is heated with an in-line gas burner.
9. The arrangement according to claim 8, characterized in that a heat exchanger is arranged to preheat air used in the gas burner.
10. The arrangement according to claim 6 or 7, characterized in that the air floatation dryer or the impingement dryer is heated with steam coils.
11. The arrangement according to any preceding claim, characterized in that the coating station is a blade coater, a curtain coater, a film coater or an air
brush coater.
12. A method for producing coated board, said method comprising
- a step of producing board in a board machine,
- a step of applying coating on the surface of said board in a coating station (11,
12, 13), and
- a step of drying said coating in a drying section (21, 22, 23),
characterized in that the coating station (11, 12, 13) is arranged online to the board machine, and the
coating is solely dried by means of air drying in the drying section (21, 22, 23).
13. The method for producing coated board according to claim 12, characterized in that, the coating is dried by at least one air dryer (21a, 21b, 21c, 22a, 22b, 22c, 23a,
23b, 23c) arranged in the drying section (21, 22, 23).
14. The method for producing coated board according to claim 12 or 13, characterized in that, the coating is applied on the surface of the board by a blade coater, a curtain
coater, a film coater or an air brush coater.