[0001] The present invention relates to paper machines. More specifically, the present invention
relates to an arrangement for improving the beginning of the drying section joined
to the closed web transfer following the press section of the paper machine, in which
paper machine: moisture is removed from the web in the press section; and the web
is transferred from the press section to a first bank of drying cylinders, in which
drying section the web will dry against the heated drying cylinder surfaces essentially
to a coating or calendering moisture content.
[0002] In paper machines, the web transfer from the press section to the drying section
is typically either open or closed, and the drying cylinders are typically cast iron
or steel cylinders.
[0003] An open web transfer means that the web travels freely from the press section to
the drying section, that is, without any support from a supporting means, such as
typically a transfer belt or felt. In connection with such an open web transfer a
drying wire is guided against the web and the web is transferred together with the
drying wire and comes into contact with the surface of a drying cylinder made of cast
iron or steel. The advantage of open web transfer is that there is hardly any working
up or formation of fluff on the web surface, whereby following the drying wire the
web will separate relatively easily from the drying cylinder surface and no essential
runability problems will occur. However, it is a problem with open web transfer that
the web receives all the tensile stress. This is why open web transfer can hardly
be used when increasing the running speeds, because with increasing running speeds
the tensile stress will grow and then there is an increased risk of web breaks and
also other runability problems will begin occurring. A web made under a higher tensile
stress will lose even all its stretching potential and the web will adhere more easily
to the drying cylinder surface, whereby the web will form a bag in the separation
zone, because the web tends to follow the drying cylinder farther than the drying
wire, which has already separated from the drying cylinder, which may result in a
web flapping phenomenon in the separation zone. Loose material or fibre fluff or bundles
may also separate more easily from a web adhering more strongly to the drying cylinder
surface, and these will adhere to the drying cylinder surface, from which they must
be removed before the drying cylinder again rotates against the web, and the web separates
less easily from the drying cylinder surface. In state-of-the-art methods of solving
the problem of how to clean the drying cylinder surface, various doctor solutions
are used which contact the drying cylinder surface. But it is a common problem with
doctors that loose material gathering behind and under the doctor will bypass the
doctor and get in contact with the web, whereby loose material will adhere to the
web, which adds essentially to the quality problems. Another problem with doctor solutions
is that the doctor blade touching the drying cylinder both becomes worn itself and,
on the other hand, it also quickly wears the drying cylinder surface. In open web
transfer from the press section to the drying section, when associated with closed
web transfer through the press section, the leader or the entire web may be run in
a controlled fashion down into the pulper immediately after the press section. The
advantage of such open web transfer is that the web's separation from the roller surface
is essentially less damaging to the web surface than separation of the web from the
transfer belt.
[0004] Closed web transfer in the press section and from the press section to the drying
section means that in the press section the web travels all the time supported by
a supporting means located above and/or under the web. From the press section to the
drying section the web is supported by a supporting means, typically a transfer belt
or felt, on the upper or bottom side of which the web is supported and it is transferred
forward from the press section. In such closed web transfer, the web is separated
from the supporting means before the drying cylinder with the aid of a suction roll,
whereby an endless supporting means loop travels around the leading roll and the web
is pressed against the drying wire travelling around the suction roll and it transfers
together with the drying wire to get in contact with the drying cylinder surface.
It is an advantage of closed web transfer that the web supporting means receives a
part of or all the tensile stress that would otherwise affect the web, whereby by
using closed web transfer it is possible to make a web with a higher stretching potential.
When the web transfer is closed in the press section and from the press section to
the drying section, the first possible place where the web can be run in a controlled
fashion down into the pulper, is the first drying cylinder. Since in connection with
closed web transfer the web is forced by suction to separate from the supporting means,
the problem arises that the web surface is worked up more strongly, that is, it becomes
fluffy. For example, fibres stand up from the web surface more strongly than in open
web transfer when the web is separated from the supporting means. Due to this fluffing
of the web, loose material, such as fibre fluff and bundles, will adhere strongly
to the drying cylinder surface made of cast iron or steel, from which they must be
removed before the drying cylinder again rotates against the web, and the web is separated
less easily from the drying cylinder surface. State-of-the-art methods try to solve
the fluffing problem by various doctor solutions touching the drying cylinder surface.
However, these have not been able to solve the problem successfully, but due to the
fluffing, which is strong at times, loose material gathered behind and under the doctor
is allowed to pass by the doctor and get in touch with the web, whereby loose material
adheres to the web, which adds essentially to the quality problems. In addition, it
is a problem with doctor solutions that the doctor blade touching the drying cylinder
surface both becomes worn and it quickly wears the drying cylinder surface. Closed
web transfer has the problem that the web's separation from the surface of the transferring
means strongly works up the web, that is, makes it fluffy, whereby the web with its
worked-up surface will adhere even more strongly to the drying cylinder surface made
of cast iron or steel, in consequence of which the web tends to follow the drying
cylinder with its rotating motion, whereby the web forms a bag in the separation zone,
because the web follows the drying cylinder farther than the drying wire, which has
already separated from the drying cylinder. Hereby loose material will adhere to the
drying cylinder surface and will increase the doctoring work and have a harmful effect
on the runability of the entire drying section and may even cause a web flapping phenomenon
in the separation zone.
[0005] When higher running speeds are the objective, increasing tensile stresses will affect
the web during the web transfer. In open web transfer the web will receive all tensile
stresses. This is why open web transfer can hardly be used at all at high running
speeds, which depending on the kind of paper are typically approximately > 1400-1700
m/min, and in addition, a web made under high tensile stresses may also lose all its
stretching potential. Closed web transfer makes possible an increased running speed,
while the tensile stresses affecting the web can also be minimised. However, in closed
web transfer at higher running speeds a problem arises in increased standing up of
fibres, that is, fluffing of the web surface, which will occur in the forced separation
of the supporting means and the web. Forced separation is brought about with the aid
of the suction of a suction roll affecting the web through the transfer means, e.g.
the drying wire. Another drawback with higher transfer speeds is that the length of
the drying section required for drying the web to coating or calendering dryness will
increase essentially. If the available hall space is limited, which is the case especially
in paper machine renewal projects, a top limit restricting the capacity is easily
formed for the production capacity which is strongly dependent on the running speed.
Surface-coated drying cylinders have earlier been suggested for use in the drying
section following the open web transfer. However, coating the drying cylinder results
in poorer heat transfer, which is why it is disadvantageous, although on the other
hand it is desirable to keep temperatures low in order to prevent burning and sticking.
However, temperatures and steam pressures are relatively low in the early part of
the drying section, so coating is of no significance to the drying capacity. This
is the very reason why the use of coating was and still is considered dubious. It
was not realised earlier, however, that coating of the drying cylinder allows using
higher temperatures without any risk of burning and sticking, which for its part allows
higher running speeds and results in added capacity.
[0006] A first objective of the present invention is to eliminate or at least to reduce
the problems relating to the known web transfer and to bring about a new and inventive
arrangement for web transfer in a paper machine after the press section. A special
objective of the present invention, along with a new and inventive arrangement, is
to:
- reduce fouling, that is, formation of fluff, on the drying cylinder,
- improve separation of the web from the drying cylinder surface,
- facilitate doctoring of the drying cylinder surface, and
- reduce wear of both the doctor touching the drying cylinder and of the drying cylinder
and to improve the doctoring tolerance of both the drying cylinder and the doctor
blade,
and in this way to allow increasing the running speed of the paper machine, to make
it possible to make a web with a higher stretching potential.
[0007] In addition, it can be said that the work to overcome friction resistance is reduced,
which reduces the need for rotating power required by the drying section, which with
increased rotating speeds may constitute a restricting factor in existing machines.
At the same time, tension variations in webs are reduced in web-driven systems. The
above-mentioned advantages are more obvious when applying the present invention to
a great number of drying cylinders.
[0008] These objectives are achieved with the arrangement mentioned in the beginning, which
is mainly characterised by the special features mentioned in the characterising part
of the independent claim.
[0009] The invention is based on the new and inventive basic idea that in order to achieve
less fouling, that is, formation of fluff, on the drying cylinder, to improve separation
of the web from the drying cylinder surface, to achieve easier doctoring of the drying
cylinder surface and a better doctoring tolerance, the surface of at least the first
drying cylinder in the drying cylinder bank is surface-coated or coated with a thin,
preferably hard coating, to which the web attaches weakly, or the drying cylinder
surface has absorbed a material, to which the web will attach weakly.
[0010] Hereby in a closed web transfer the supporting means of the web will receive entirely
or at least partly the tensile stress applied to the web; the web will separate essentially
without effort together with the drying wire from the drying cylinder surface; less
loose material or fibre fluff or fibre bundles will separate from the web on to the
drying cylinder surface; and less cleaning is needed with a doctor stressing the drying
cylinder surface.
[0011] In accordance with an advantageous embodiment of the invention, a coating, which
is chosen so that adherence of the web to the drying cylinder surface is made as weak
as possible, is a ceramic material or metal ceramic or a mixture or compound of these.
The coating may also be a mixture of the above-mentioned ceramic materials or of metal
ceramics and a metal. Such a ceramic material or metal ceramic coating, the thickness
of which is preferably in a range between 0.03 and 6 mm, can be sprayed thermally
on to the roll surface, and in order to ensure adhesion a thin adhesive layer may
be used between the coating and the coat iron or steel surface of the cylinder. Alternatively,
in order to facilitate the web's separation from the surface, the porous drying cylinder
surface may be covered or coated with fluorated plastic or with fluorated epoxy, which
has the same properties as fluoroplastic, either alone or in addition to the above-mentioned
coating.
[0012] In the following, the invention will be described by way of example with the aid
of a preferable embodiment and referring to the appended drawings, wherein
FIG. 1 is a schematic side view of web transfer from the press section to the drying
section in a paper machine;
FIG. 2 is a graphic view of the paper web's separation force from different drying
cylinder surfaces as a function of the separation angle; and
FIG. 3 is a schematic cross-sectional view of a drying cylinder according to the invention.
[0013] Figure 1 is a schematic view of the press section 1 in a paper machine, wherein water
is pressed out of web W and wherein a closed web transfer is arranged for web W through
the press section 1 to the drying section 3. In the drying section 3, web W is dried
to a solids content required by the web treatment after the drying section, such as
e.g. coating or calendering or reeling etc.
[0014] In the press section 1, web W travels through press rolls 14 and 15 in between a
press felt 10 and a transfer means 4. In figure 1 the press felt 10 is illustrated
by a line of dots and dashes and the endless loop which it forms travels around the
leading rolls 12 of the press felt 10. The transfer means 4 is preferably a transfer
belt impervious to liquid and/or air, but it may also be a press felt or equivalent,
and in Figure 1 it is illustrated by a dashed line. Transfer belt 4 forms an endless
loop, which travels around leading rolls 13. After press rolls 14 and 15, press felt
10 is separated from web W, whereupon the web is held on to transfer means 4, which
supports it.
[0015] Thus, in press section 1 the web proceeds in closed web transfer on the transfer
means 4 to the drying unit 3. In the travelling direction of the web, that is, in
the MD direction of the paper machine, the press unit 1 is followed by a suction roll
5, around which a drying wire 8 is turning. Suction affecting in the suction zone
of suction roll 5 forces the web W against the drying wire 8, which in Figure 1 is
illustrated by a dotted line, and along with this to a first drying cylinder 6
1. In the MD direction the suction roll 5 is followed, preferably immediately, by the
leading roll 13 of the transfer means 4, and the leading roll is used to guide the
travel of transfer means 4 away from the bottom surface of web W.
[0016] After suction roll 5, web W travels supported against the bottom surface of drying
wire 8 to the first bank of drying cylinders of drying unit 3 and into direct contact
with the heated cylinder surface of the first drying cylinder 6
1. After the first drying cylinder 6
1 of the first bank of drying cylinders, web W turns around hitch roll 7, whereby drying
wire 8 is against the cylinder surface of the hitch roll and web W is outside drying
wire 8, to the second drying cylinder 6
2 of the first bank of drying cylinders. Thus, the endless drying wire loop revolving
in the first bank of drying cylinders in the drying section travels both by way of
the leading rolls 41 of drying wire 8 and also around suction roll 5, the first drying
cylinder 6
1 and the first hitch roll 7, and after the first drying cylinder-hitch roll pair 6
1, 7 it zigzags around the following drying cylinder-hitch roll pairs 6
n, 7.
[0017] In order to achieve less fouling of drying cylinders 6
1-n, that is, less formation of fluff on the same, to improve the separation of web W
from the surface of drying cylinders 6
1-n, to achieve easier doctoring and a better tolerance of doctoring of the surface of
drying cylinders 6
1-n, the surface of at least the first drying cylinder 6
1 of the drying cylinder bank is surface-coated or coated with a thin, preferably hard
coating 60. In order e.g. to fill pores or roughness, a coating 60, to which the web
will adhere weakly, is absorbed into the surface of the drying cylinder 6
1-n made alternatively or optionally of cast iron or with a surface of some other material
or with a hard-coated surface. Thus, the absorption material 60 hereby need not cover
the metal surface of the drying cylinder 6
1-n uniformly and everywhere. In accordance with the invention, the surface-coating or
coating or absorption material 60 is chosen so that web W will adhere weakly to the
surface-coating or coating or absorption material 60. Hereby web W separates together
with drying wire 8 essentially effortlessly from the surface of drying cylinder 6
1-n and less loose material or fibre fluff or fibre bundles will separate from web W
on to the surface of drying cylinder 6
1-n, which again reduces the cleaning work to be done on the surface of drying cylinder
6
1-n with a doctor 9
1a and with a secondary doctor 9
1b.
[0018] When the web transfer is closed in the press section 1 and from the press section
1 and further to the drying section 3, the first possible place where the entire web
W can be run in a controlled fashion down into pulper 31, is the first drying cylinder
6
1 after suction roll 5. Hereby it must be possible to doctor the surface of drying
cylinder 6
1 strongly and the web must also separate from the surface of the first drying cylinder
6
1 without passing through and past the doctor or doctors 9
1a, 9
1b.
[0019] Figure 1 shows in connection with the first drying cylinder two successive doctors
9
1a, 9
1b to ensure that all loose material or the leader or the whole web is safely separated
from the surface of drying cylinder 6
1 and guided into the pulper 31 located below.
[0020] The surface-coating in accordance with the invention is arranged in the drying unit
in the first drying cylinder 61 of at least the first bank of drying cylinders. It
should be emphasised, that in order to minimise adherence and to minimise the need
for doctoring, the surface-coating or coating of the surface or absorption of the
surface according to the invention may also be arranged in the following drying cylinders
6
2- n. Hereby it is possible to reduce the cleaning work stressing the surface of drying
cylinders 6
2-n, which is to be performed in the whole drying unit by all doctors 9
2-n. Another noteworthy advantage is achieved in that loose material or fibre fluff or
fibre bundles separate less than before in connection with the cleaning work, whereby
less loose material of all kinds is gathered in pulper 31 as a result of the doctoring
work. The work to overcome friction resistance is also reduced, which reduces the
drying section's need for rotating power, which may form a restricting factor in existing
machines with increasing speeds of rotation. At the same time, tension variations
in webs are reduced in web-driven systems. The above-mentioned advantages are the
more obvious when the present invention is applied to more drying cylinders.
[0021] Figure 3 is a schematic cross-sectional view of the drying cylinder 6
1 according to the invention. The coating 60 according to an advantageous embodiment
of the invention of drying cylinder 6
1 includes or the coating 60 consists of a hard layer 602 of a ceramic material, which
is preferably oxide ceramic, such as Zr, Al, Si, Ti, Y, Cr oxide ceramics, or carbide
ceramic, such as Cr, W, Ti, Ni carbide ceramics. According to the invention, the hard
layer 602 may also consist of a mixture or compound of the above-mentioned ceramic
materials. Furthermore, the hard layer 602 of coating 60 may according to the invention
also be a mixture or compound of the above-mentioned ceramic materials and a metal,
preferably chrome, nickel and/or molybdenum. Such mixtures and compounds are generally
known by the name of metal ceramics or cerametals or cermet.
[0022] According to the invention, the hard layer 602 of coating 60 may be made not only
of a ceramic material or metal ceramics, but also of a metal, which preferably is
chrome, molybdenum and/or nickel,
[0023] The thickness of the ceramic material or metal ceramics coating 60 forming the hard
layer 602 of coating 60 is preferably in a range of 0.03-6 mm, most preferably in
a range of 0.05-2 mm.
[0024] Such a coating 60 can be spread out by plasma spraying or by HVOF (High Velocity
Oxy Fuel) spraying thermally on to the roll surface, whereby a surface of ceramic
material or metal ceramics is formed. In order to ensure adherence between coating
60 and the surface, for example, such as a cast iron or steel surface, of drying cylinder
6
1-n, a thin adhesive layer 601 may be used, which is e.g. a non-porous metal layer, which
thus does not have any essential effect on the total thermal conductivity of the drying
cylinder and which functions as a protective layer against corrosion at the same time.
[0025] According to a particularly advantageous embodiment of the invention, to promote
separation of the web from the surface, fluorated plastic, preferably PTFE (Polytetrafluoroethylene,
a known trademark of which is TEFLON®), or fluorated epoxy with the same properties
as PTFE, may be absorbed according to the invention into the surface pores or surface
profile roughness of the drying cylinder made of cast iron or steel or of the hard
layer 602 consisting of a layer of ceramic material and/or metal ceramics and/or metal,
to coat or surface-coat the drying cylinder. Of the optional alternatives it is most
advantageous that the cast iron or steel surface of the drying cylinder is first surface-coated
with the above-mentioned hard coating 602, which is made to adhere to the drying cylinder
surface by an adhesive layer 601. Because the hard coating 602 leaves the outer surface
porous, fluorated plastic or fluorated epoxy may be absorbed into the pores of the
hard surface.
[0026] When fluorated plastic or fluorated epoxy is also absorbed into the coating 60 of
the drying cylinder including a hard layer 602, the coating 60 according to the most
preferable embodiment of the invention consists of a PTFE coated ceramic material
or of PTFE coated metal ceramics.
[0027] The cylinder may also be surface-coated by coating the cylinder surface with fluorated
plastic, which is preferably PTFE, with a coated metal layer, wherein the metal is
preferably nickel, chrome or molybdenum. Hereby the coating is a PTFE coated metal.
[0028] Figure 2 is a graphic view of the paper web's separation force from different drying
cylinder surfaces as a function of the separation angle based on test runs carried
out at a production velocity of 22 m/s. From the viewpoint of the invention, the most
essential coatings are the following, besides metal coatings:
a. ceramic material coatings, such as Zr, Al, Si, Ti, Y and Cr oxide based oxide ceramic
and Cr, W, Ti and Ni carbide based carbide ceramic, e.g. nitride and boride ceramics
are also useable ceramics,
b. metal ceramic coatings, which are typically mixtures of oxide or carbide ceramics
and metal, preferably Cr, Ni, Mo,
c. metal coatings, preferably Cr, Ni and Mo coatings, as well as
d. PTFE coated hard coatings, which according to the invention are e.g.
i. PTFE coated ceramic materials, whereby
a) the oxide ceramic is preferably Zr, Al, Si, Ti, Y or Cr oxide, and/or
b) the carbide ceramic is preferably Cr, W, Ti or Ni carbide,
ii. PTFE coated hard coatings, whereby preferably
a) the oxide ceramic is e.g. Zr, Al, Si, Ti, Y or Cr oxide and the metal is Cr, Ni
or Mo, and/or
b) the carbide ceramic is e.g. Cr, W, Ti or Ni carbide and the metal is Cr, Ni or
Mo
iii. PTFE coated metals, whereby the metal is e.g. Cr, Ni or Mo.
[0029] Figure 2 illustrates the separation force of the paper web from surfaces, which are:
i. a PTFE nickel surface representing a PTFE coated metal coating,
ii. an aluminium oxide ceramic surface representing ceramic material coating, and
iii. a tungsten carbide cobalt surface representing metal ceramic coating.
[0030] In addition, Figure 2 illustrates for the sake of comparison the separation force
of the paper web from a cylinder surface made of cast iron or steel at a corresponding
production velocity.
[0031] As can be seen in Figure 2, with each coating according to the invention the paper
web separates from the coated cylinder surface with an essentially lower separation
force than from a cylinder surface made of cast iron or steel. Hereby the risk of
fluff formation is reduced and that way also fouling of the cylinder surface.
[0032] The invention was described above only by way of example with the aid of its one
mode of application, which is considered advantageous. Of course, this does not mean
any intention to limit the invention in any way to concern such an individual example
only, and as is obvious to the professional in the art, alternative solutions and
modifications are possible within the scope of the new and inventive idea defined
in the appended claims.
[0033] Thus it should be noted that between the press section and drying section shown in
Figure 1 it is possible to arrange one or more desired units, e.g. a web transfer
and/or pre-drying unit, on to which the web is taken from the press section as closed
web transfer and from which the web is taken further as closed web transfer to the
drying section, the first drying cylinder of which is a coated drying cylinder in
accordance with the invention.
[0034] The above description and the following claims are based essentially on the following
terminology and concepts:
1. metal:
i. a metallic material or a metal alloy
2. ceramic material:
ii. a ceramic material, such as oxide or carbide ceramic, or a mixture or compound
of ceramic materials
3. oxide ceramic:
iii. a ceramic formed by oxidisation, usually a metal oxide
4. carbide ceramic:
iv. a carbide usually formed by carbon and a metal
5. metal ceramic:
v. a mixture or compound of a ceramic material and a metal
1. Arrangement for improving the beginning of the drying section (3) joined to closed
web transfer after the press section (1) in a paper machine, in which paper machine:
moisture is removed from the web (W) in the press section (1); and the web is guided
from the press section to the first bank of drying cylinders of the drying section
(3), in which drying section (3) the web dries against heated drying cylinder surfaces
essentially to the solids content required for treatment of the web after the drying
section (3), such as e.g. coating or calendering or reeling or other such, characterised in that in order to achieve less fouling of the drying cylinder (61-n), that is, less fluff formation, to achieve better doctorability and better doctoring
tolerance of the drying cylinder (61-n) surface in the drying section (3) there is a coating (60) on the surface of at least
the first drying cylinder (61), which coating includes a thin, preferably hard layer (602) of ceramic material
and/or metal ceramic and/or metal, to which the web will adhere weakly, and/or another
softer material (603), to which the web will adhere weakly is absorbed into the drying
cylinder (61-n) surface, whereby separation of the web (W) from the surface of the drying cylinder
(61-n) is improved.
2. Arrangement as defined in claim 1, characterised in that at least the first two drying cylinders (61-n) of the drying section (3) include a thin preferably hard coating layer (60) of a
ceramic material and/or metal ceramic and/or metal.
3. Arrangement as defined in claim 1 and/or 2, characterised in that fluorated plastic or fluorated epoxy (603) is absorbed into the surface of the drying
cylinder (61...n).
4. Arrangement as defined in claim 3, characterised in that the fluorated plastic is polytetrafluoroethylene.
5. Arrangement as defined in claim 1 and/or 2, characterised in that the coating (60) of the drying cylinder (61...n) made of cast iron or steel includes a lower hard layer (602), which is of a ceramic
material, metal ceramic and/or metal, and a softer layer (603) of fluorated plastic
or epoxy of the kind absorbed into the hard layer (602).
6. Arrangement as defined in claim 1 and/or 2, characterised in that the coating (60) consists of a hard layer (602) only, which is ceramic material,
metal ceramic and/or metal.
7. Arrangement as defined in any one of claims 1-6, characterised in that the ceramic material (602) forming the hard layer (602) of the coating (60) is oxide
ceramic, preferably Zr, Al, Si, Ti, Y or Cr oxide ceramic, and/or carbide ceramic,
preferably Cr, W, Ti or Ni carbide ceramic.
8. Arrangement as defined in any one of claims 1-6, characterised in that the metal ceramic forming the hard layer (602) of the coating (60) is a mixture or
compound of an oxide ceramic, which is preferably Zr, Al, Si, Ti, Y or Cr oxide ceramic,
and/or a carbide ceramic, which is preferably Cr, W, Ti or Ni carbide ceramic, and
a metal, which is preferably Cr, Ni or Mo.
9. Arrangement as defined in any one of claims 1-6, characterised in that the metal forming the hard layer (602) of the coating (60) is preferably Cr, Ni or
Mo.
10. Arrangement as defined in any one of claims 1-6,
characterised in that the lower hard layer (602) of the coating (60) is a mixture or compound of at least
two materials, which materials have been chosen from a set including:
- oxide ceramics, preferably Zr, Al, Si, Ti, Y and Cr oxide ceramics,
- carbide ceramics, preferably Cr, W, Ti and Ni carbide ceramics,
- metal ceramics, preferably Zr, Al, Si, Ti, Y and Cr oxide ceramics, and/or mixtures
or compounds of Cr, W, Ti or Ni carbide ceramics and metals, preferably Cr, Ni or
Mo, and
- metals, preferably Ni, Cr and Mo,
and that a softer layer (603) of fluorated plastic, such as PTFE, and/or fluorated
epoxy, is absorbed into the surface of the hard layer (602).
11. Arrangement as defined in any one of claims 1-10, characterised in that the thickness of the hard layer (602) of a ceramic material and/or a metal ceramic
in the coating (60) is preferably in a range of 0.03-6 mm, most preferably in a range
of 0.05-2 mm.
12. Arrangement as defined in any one of claims 1-11, characterised in that the hard layer (602) of the coating (60) is sprayed thermally on to the surface of
the drying cylinder (61-n) and that to ensure adhesion an adhesive layer (601), which is preferably a non-porous
metal layer, is used in between the hard layer (602) of the coating (60) and the cast
iron or steel cylinder surface of the drying cylinder (61, 62, 6n).
13. Arrangement as defined in any one of claims 1-12, characterised in that fluorated plastic is absorbed into the coating (6) including the hard layer (602),
whereby the coating (60) consists of a PTFE coated ceramic material or of a PTFE coated
metal ceramic or of a PTFE coated metal.