WO2002095125A1 - Method and cylinder for heating or cooling of a fibrous web - Google Patents

Method and cylinder for heating or cooling of a fibrous web Download PDF

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Publication number
WO2002095125A1
WO2002095125A1 PCT/FI2002/000447 FI0200447W WO02095125A1 WO 2002095125 A1 WO2002095125 A1 WO 2002095125A1 FI 0200447 W FI0200447 W FI 0200447W WO 02095125 A1 WO02095125 A1 WO 02095125A1
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WO
WIPO (PCT)
Prior art keywords
cylinder
heat transfer
heat
cylinder wall
fibrous web
Prior art date
Application number
PCT/FI2002/000447
Other languages
French (fr)
Inventor
Pertti Heikkilä
Original Assignee
Metso Paper, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Metso Paper, Inc. filed Critical Metso Paper, Inc.
Publication of WO2002095125A1 publication Critical patent/WO2002095125A1/en

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Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00—Dryer section of machines for making continuous webs of paper
    • D21F5/02—Drying on cylinders
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00—Dryer section of machines for making continuous webs of paper
    • D21F5/02—Drying on cylinders
    • D21F5/022—Heating the cylinders
    • D21F5/028—Heating the cylinders using steam
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21G—CALENDERS; ACCESSORIES FOR PAPER-MAKING MACHINES
    • D21G1/00—Calenders; Smoothing apparatus
    • D21G1/02—Rolls; Their bearings
    • D21G1/0253—Heating or cooling the rolls; Regulating the temperature
    • D21G1/0266—Heating or cooling the rolls; Regulating the temperature using a heat-transfer fluid

Definitions

  • the present invention relates to a method and a cylinder for heating or cooling a fibrous web, as defined in the preamble of the enclosed independent claims.
  • the fibrous web is dried in the drying section of the machine by guid- ing the web over one or more heated drying cylinders, usually in direct heat transfer contact with the shell surface of the cylinders.
  • the fibrous web is thereby dried by conducting heat from the drying cylinder or cylinders to the web, so that the desired amount of water evaporates from the web and the web reaches the desired dry matter content.
  • Soft paper like kitchen paper or other sanitary paper, is usually made in machines having a single large drying cylinder, e.g. a so-called Yankee dryer, or in machines having both conventional drying cylinders and one or more larger drying cylinders.
  • the diameter of the large drying cylinders is > 2 m, usually 3 to 6 m.
  • the large drying cylinders may have a plain shell surface, e.g. in order to make crepe paper, or a patterned shell surface, e.g. in order to make structured soft paper.
  • the drying cylinders are heated by steam, whereby the steam transfers heat to the web in an amount which is required to evaporate the desired amount of water from the web as it is guided over the shell surface of the cylinder.
  • Yankee dryers are dimensioned utilizing an optimal ratio between steam pressure and cyl- inder wall thickness in order to obtain maximal heat transfer.
  • a steam pressure of 5 to 10 kPa results in a maximal heat transfer for the cylinder sizes in question.
  • a disadvantage of large drying cylinders, particularly the Yankee dryers, is their actual size. Due to production problems it is at present almost impossible to increase the drying capacity by further increasing the diameter of a Yankee dryer. Also the transport arrangements for the transport of very large cylinders can create an obstacle for a further increase of the cylinder size. Another problem is presented by the great material thickness of the cylinders, which reduces the heat transfer from the internal space of the cylinder to its shell surface.
  • a Yankee dryer for tissue machines is usually provided with internal notches or grooves in the peripheral direction of the cylinder. The shell thickness can be about 100 mm before the grooves are turned in the inner surface of the shell. In a new grooved cylinder this thickness remains between the grooves.
  • this thickness is reduced to a value somewhere between 50 and 70 mm.
  • the thickness at the bottom of the grooves will also be reduced, and usually it can be allowed to be reduced to a value slightly less than 25 mm.
  • An MG cylinder which is plain on the inside can have a thickness of about 40 to 60 mm when it is new. By regrinding the thickness of the shell can be allowed to be reduced to a value slightly less than 25 mm in order to withstand the internal steam pressure in the cylinder.
  • a Yankee dryer Due to the shell surface thickness and the large diameter of the cylinder a Yankee dryer therefore has a considerable mass which must be heated by the steam. The great thickness reduces the heat transfer to the shell surface of the cylinder. Due to this it is difficult to obtain the sufficiently high heat flow required by the drying through the shell surface of a Yankee dryer, and therefore the temperature on the shell surface usually is 95 to 100 °C at the most.
  • a further problem encountered when the diameter of a Yankee dryer is increased is the difficulty to keep the same temperature on the cylinder shell and the cylinder ends, so that the shape of the cylinder remains constant in the machine cross direction. Temperature differences can result in high tensions between the shell surface and the ends as they are not able to expand freely and independently of each other.
  • the object of the present invention is to provide a method and a cylinder for heat- ing or cooling a fibrous web where the above-mentioned disadvantages are minimised.
  • An object is then also to increase the heat transfer capacity in a machine for heating or cooling a fibrous web with a cylinder without essentially increasing the space required for the heat transfer.
  • An object is also to provide a way to increase the heat transfer capacity of drying cylinders without necessarily increasing the size of the cylinder or without using additional energy in order to heat the shell surface of the cylinder.
  • An object is also to use a heat transfer liquid instead of steam. It is essential that the heat transfer medium remains in liquid form during the entire heat transfer process. An object is also that the heat emission is based on heat energy, which the liquid emits when cooling. An object is also to use a closed system whereby the pressure in the piping system is close to the atmospheric pressure, and to use a liquid having a boiling point clearly above 100 °C, typically at least near 400 °C or even higher.
  • a typical method for heating, drying or cooling a fi- brous web in the making or treating of a fibrous web in a machine having at least one cylinder, which heats or cools the fibrous web, in which cylinder the wall is made of metal or some other suitable heat transferring material, whereby the fibrous web is guided over the heating or cooling cylinder in a heat transfer contact with at least a part of the shell surface of the cylinder, whereby the medium heat- ing or cooling the shell surface of the cylinder is a heat transfer liquid, such as heat transfer oil or the like which remains in liquid form during the heat transfer process.
  • the steam pressure of the liquid is less than 80 kPa within the temperature range that is relevant for the implementation of the method. Thereby the initial boiling point is typically above the upper limit of this temperature range.
  • the medium heating or cooling the shell surface of the cylinder is conducted through the cylinder in passages in direct or indirect heat transfer contact with the cylinder wall.
  • a typical cylinder for the heating or cooling a fibrous web in a machine for the making or treating of the fibrous web comprises a cylinder wall of metal or some other suitable material which transfers heat, end walls, and passages for conducting a heat emitting or heat receiving medium through the cylinder.
  • the passages for conducting the heat emitting or heat receiving medium through the cylinder are typically passages formed in the material of the cylinder wall, or passages arranged at or in the cylinder wall, in order to conduct the medium heating or cooling the shell surface of the cylinder through the cylinder in direct or indirect heat transfer contact with the cylinder wall.
  • the heat emitting or receiving heat transfer medium comprises a heat transfer liquid, such as heat transfer oil or the like, which remains in liquid form during the heat transfer process.
  • the steam pressure of the liquid is less than 80 kPa within the temperature range that is relevant for the implementation of the heat transfer between the heat transfer liquid and the cylinder.
  • the initial boiling point of the heat transfer liquid is thereby typically above the upper limit of this temperature range.
  • tissue machines are thereby utilized advantageously heat transfer liquids having an initial boiling point above 250 °C, suitably above 300 °C, preferably above 350 °C, and having preferably a vapour pressure lower than 10 kPa at 300 °C.
  • heat transfer oils with a temperature > 100 °C, typically 150 to 300 °C, can be suitably used as the heat transfer medium in drying cylinders.
  • Heat transfer oil could be sprayed on the inner surface of the cylinder and removed from the cylinder in a suitable way, e.g. with a siphon, in a similar way as water- steam condensate is removed from conventional drying cylinders with the aid of a pressure difference.
  • the heat exchange oil could be removed out of the cylinder by designing the cylinder as a pressure vessel, or with a pump and a suction pipe.
  • the inner surface of the cylinder can be provided with radial or axial grooves or grooves in the direction of the shell pe- riphery.
  • a more effective heat transfer is obtained if the heat transfer oil is conducted through tubes, heat exchanger tubes, which are in contact with the inner surface of the cylinder wall.
  • This practice requires a good heat transfer contact between the heat exchanger tubes and the cylinder wall.
  • a good contact can be obtained by fill- ing the space between the heat exchanger tubes and the cylinder wall with some material having good heat transfer characteristics.
  • other metals or filling materials which provide a good heat transfer contact between tubes and cylinder wall could be used.
  • axial grooves shaped in the inner wall of the cylinder can provide the passages for the heat transfer oil.
  • the grooves can be covered by an additional inner cylindrical plate or inner wall so that separate passages are formed in the wall of the cylinder. It is also possible to shape separate passages in the actual wall material, e.g. by drilling passages in it.
  • the passages formed in the cylinder wall are mainly in parallel with the cylinder axis, and all of them are arranged separately or in groups at an equal distance from the cylinder axis.
  • the diameter of the passages formed in the cylinder wall or the passages arranged at or in the cylinder wall can be mainly constant in the direction of the cylinder axis, but on the other hand the diameter can be, if so desired, e.g. increasing in the flow direction in order to maintain a constant heat transfer from the heat transfer oil or the like to the shell surface of the cylinder, despite the temperature change in the flow direction.
  • heat transfer oil or other suitable heat transfer material is supplied into a drying cylinder through an inlet at one axle journal of the cylinder, and distributed from it via a manifold arranged at the inner wall of the cylinder, for example on the drive side of the cylinder, to passages formed in the cylinder wall or to heat exchanger tubes arranged at or in the cylinder wall.
  • a collector which collects the heat transfer oil or the like from the heat exchanger tubes or passages in order to be drained through an outlet arranged in the other axle journal.
  • the heat transfer medium should not be cooled or heated too much as it flows through the cylinder.
  • the heat transfer medium can be suitably cooled about 10 °C as it flows through the cylinder.
  • the cooling of the heat transfer medium can be compensated for by making the cylinder wall slightly conical, so that the walls at the inlet side are for instance 10 % thicker than at the outlet side, which will compensate for the temperature change between the inlet and outlet sides.
  • Another alternative way to compensate for the temperature changes is to allow the heat transfer medium to flow in a first direction in every second heat exchanger tube and in the opposite direction in the other tubes.
  • Figure 1 shows a schematic cross section through a part of a cylinder's cylinder wall according to the invention
  • Figure 2 shows a schematic cross section through a part of another cylinder's cylinder wall according to the invention
  • Figure 3 shows schematically an axial cross section of a cylinder according to the invention
  • Figure 4 shows a schematic flow diagram for the heat transfer medium between a drying cylinder and an apparatus for heating the heat transfer medium.
  • FIG 1 a cross section of a sector of the cylinder wall 10 in a drying cylinder.
  • a number of heat exchanger tubes 14 are arranged in the cylinder wall at its inner side 12.
  • the tubes 14 are arranged in parallel with the cylinder axis and at an equal distance from the axis.
  • the tubes 14 are fastened to the inner side 12 of the cylinder wall with the aid of hot galvanizing with zinc 16, which partly encircles the tubes and fills the space between the tubes and the inner side of the cylin- der wall.
  • the galvanizing with zinc provides a good heat transfer contact between the tubes and the inner side of the cylinder wall.
  • Hot heat transfer oil is arranged to flow through the tubes, whereby heat is transferred from the oil via the tube wall, the zinc layer and the cylinder wall to the shell surface 18 of the cylinder, in order to heat that fibrous web which is to be dried by the drying cylinder.
  • FIG 1 is shown an advantageous embodiment of the invention in heating and drying of a fibrous web, such as a soft paper web, according to which the heat emitting, heating and drying medium is conducted through the drying cylinder in heat transferring contact with the cylinder wall through heat exchanger tubes arranged at the inner surface of the cylinder wall or in the cylinder wall.
  • a good heat transfer contact between the heat exchanger tubes and the cylinder wall is obtained by adding material with good heat transfer characteristics between the cylinder wall and the tubes arranged at its inner surface.
  • the heat exchanger tubes can e.g. be fastened to the cylinder wall by hot galvanizing with zinc.
  • FIG 2 is shown an alternative embodiment according to the invention for the heating of the shell surface 18 of a drying cylinder.
  • the inner side 12 of the cylinder wall 10 has passages 14 formed in the actual material of the cylinder wall.
  • the passages 14 are covered by a thin inner cylinder 20 forming a wall which closes the passages, so that separate tube-like passages are formed at the inner wall of the drying cylinder, partly embedded in the wall material.
  • Figure 2 shows an advantageous embodiment of the invention in heating and dry- ing a fibrous web, such as a soft paper web, according to which the heat emitting, heating and drying medium is conducted through the drying cylinder in direct or indirect heat transfer contact with the cylinder wall via passages formed in the material of the cylinder wall.
  • FIG 3 shows an axial cross section of a drying cylinder 22 according to the invention.
  • An inlet 28 for heat transfer medium m is arranged through a first axle journal 26 at the first end 24 of the drying cylinder, and an outlet 34 for the heat transfer medium is arranged through the second axle journal 32 at the second end 30.
  • the inlet 28 is connected to a manifold 36 arranged at the inner side of the first end.
  • the outlet 34 is connected to a collector 38 arranged at the inner side of the second end.
  • the manifold 36 and the collector 38 are interconnected by heat exchanger tubes or passages 14, for example of that type shown in figures 1 and 2.
  • Heat transfer liquid such as heat transfer oil
  • Heat transfer oil is arranged to flow at a temperature of > 100 °C, preferably 150 to 300 °C, from the inlet 28 via the manifold 36, the tubes or passages 14, the collector 38 and the outlet 34, through the drying cylinder 22, in order to heat the shell surface 18 of the cylinder.
  • FIG. 4 shows a system for heating the shell surface 18 of a drying cylinder 22.
  • the heat transfer medium is in this case heat transfer oil.
  • 230 kg/s oil at a temperature of 220 °C is supplied into the drying cylinder 22 via an inlet 28.
  • the oil flows through tubes or passages 14 and emits heat through the cyl- inder wall to the shell surface 18 of the cylinder, after which the oil flows out from the cylinder via the outlet 34 at a temperature of about 210 °C.
  • the main part of the drained oil, 197 kg/s is conducted via a circulation line 38, a valve 40 and an inlet line 42 with a pump 44, back to the inlet 28 of the drying cylinder 22.
  • a partial flow, 33 kg/s, of the drained oil is conducted via a line 46 to a heating appara- tus 48, where the oil is heated to a temperature of 280 °C.
  • the heated oil is conducted via a line 50 to the valve 40 in order to be supplied to the inlet line 42 together with the main part of the oil.
  • the partial flow of heated oil is mixed together with the main part of oil, which provides a flow of 230 kg/s oil at a temperature of 220 °C in the inlet line. According to this system only a part of the oil must be circulated through the heating apparatus.
  • the temperature of that oil which is supplied in the drying cylinder can be rapidly adjusted by adjusting, in a way known as such, the ratio between the two oil flows, the main flow and the partial flow.
  • the heat transfer oil remains in liquid form during the heat transfer process.
  • the aim of the following example is to show that with a drying cylinder according to the invention there can be obtained the same or an substantially higher, e.g. 50 % higher, heat transfer rate than with a conventional steam heated drying cylinder.
  • the oil-heated cylinder is assumed to be designed so that it emits 50 % more heat than the steam-heated cylinder;
  • the temperature of the shell surface of the steam-heated cylinder is 100 °C;
  • the temperature of the shell surface of the oil-heated cylinder is 110 °C.
  • the outer/inner diameter of the heat exchanger tubes is assumed to be 21/17 mm, and the tube distance at the cylinder wall to be 28 mm. Thus the wall contains 504 tubes in total. Thus the oil flow in the tubes is 2.2 m/s.
  • the heat transfer coefficient from the oil to the inner wall of the tube is 1.55 kW/m /°C.
  • the thermal conductivity of the wall is assumed to be 50 W/m/°C.
  • a wall thickness of 39 mm from the bottom of the groove to the ex- ternal surface of the cylinder provides the mentioned k-value 0.7 kW/m /°C, which shows that with oil heating it is possible to achieve a corresponding k-value as with steam heating of a cylinder.
  • the present invention proposes that drying cylinders are heated with heat transfer oil or a corresponding medium instead of steam, which medium does not evaporate at the temperature and pressure in question.
  • heat transfer oils of different types, which can be used at temperatures of up to 300 °C and which are suitable for heating purposes in different embodiments of the invention, are available.
  • suitable heat transfer oils can be mentioned as an example Thermia B and Thermia E from Shell.
  • the initial boiling point of Thermia B is about 355 °C, and of Thermia E about 410 °C.
  • the temperature of the heat emitting surface should not exceed 340 °C.
  • the steam pressure of Thermia B is hardly 10 kPa, and at 220 °C it is less than 1 kPa.
  • the steam pressure of Thermia E is lower.
  • drying cylinder It is not necessary to dimension the drying cylinder as a pressure vessel.
  • the temperature level can be raised from the present level to a higher temperature level without increasing the size of the actual drying cylinder construction.
  • the invention can be utilized to increase the drying capacity of large drying cylinders, for example of the Yankee dryer type, having a large diameter > 2 m, usually 3 to 6 m.
  • the invention can be utilized for example in Yankee dryers in tissue machines.
  • the drying capacity of the cylinder can be controlled in a simple manner by adjusting the temperature of the oil.
  • the invention can be utilized as well in large cylinders with a plain surface for the making of e.g. crepe paper, as in large cylinders with a patterned surface for making of structured soft paper.
  • the invention can also be applied in conventional drying sections in paper machines.
  • the capacity of existing drying sections can be increased by replacing conventional steam-heated cylinders with oil-heated cylinders of the same size.
  • the invention can also be advantageously utilized in cylinders which cool fibrous webs, whereby the heat transfer medium, in this case the cooling medium, is cold water.
  • the cylinder provides an improved heat transfer effect or a lower water consumption.
  • the drying cylinders are typically made of metal, such as steel or cast iron.

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Abstract

A method and a cylinder (22) for heating or cooling a fibrous web in the making or treating of a fibrous web in a machine having at least one cylinder, which heats or cools the fibrous web. The shell surface (18) of the cylinder is heated or cooled with heat emitting or heat receiving medium (m) which is conducted through the cylinder in direct or indirect heat transfer contact with the cylinder wall. The medium heating or cooling the shell surface of the cylinder is a heat transfer liquid having a steam pressure lower than 80 kPa within the temperature range that is relevant to the implementation of the method.

Description

Method and cylinder for heating or cooling of a fibrous web
The present invention relates to a method and a cylinder for heating or cooling a fibrous web, as defined in the preamble of the enclosed independent claims.
In a conventional paper machine or an other corresponding machine for making fibrous webs the fibrous web is dried in the drying section of the machine by guid- ing the web over one or more heated drying cylinders, usually in direct heat transfer contact with the shell surface of the cylinders. In the drying section the fibrous web is thereby dried by conducting heat from the drying cylinder or cylinders to the web, so that the desired amount of water evaporates from the web and the web reaches the desired dry matter content.
Soft paper, like kitchen paper or other sanitary paper, is usually made in machines having a single large drying cylinder, e.g. a so-called Yankee dryer, or in machines having both conventional drying cylinders and one or more larger drying cylinders. The diameter of the large drying cylinders is > 2 m, usually 3 to 6 m. The large drying cylinders may have a plain shell surface, e.g. in order to make crepe paper, or a patterned shell surface, e.g. in order to make structured soft paper.
Normally the drying cylinders are heated by steam, whereby the steam transfers heat to the web in an amount which is required to evaporate the desired amount of water from the web as it is guided over the shell surface of the cylinder. Yankee dryers are dimensioned utilizing an optimal ratio between steam pressure and cyl- inder wall thickness in order to obtain maximal heat transfer. A steam pressure of 5 to 10 kPa results in a maximal heat transfer for the cylinder sizes in question.
There are numerous patent publications which present different constructions in the prior art, for instance FI 106054, FI 105115, FI 103679, FI 100121 and FI 91297.
However, one disadvantage of large drying cylinders, particularly the Yankee dryers, is their actual size. Due to production problems it is at present almost impossible to increase the drying capacity by further increasing the diameter of a Yankee dryer. Also the transport arrangements for the transport of very large cylinders can create an obstacle for a further increase of the cylinder size. Another problem is presented by the great material thickness of the cylinders, which reduces the heat transfer from the internal space of the cylinder to its shell surface. A Yankee dryer for tissue machines is usually provided with internal notches or grooves in the peripheral direction of the cylinder. The shell thickness can be about 100 mm before the grooves are turned in the inner surface of the shell. In a new grooved cylinder this thickness remains between the grooves. When the cylinder has been reground a number of times this thickness is reduced to a value somewhere between 50 and 70 mm. The thickness at the bottom of the grooves will also be reduced, and usually it can be allowed to be reduced to a value slightly less than 25 mm. An MG cylinder which is plain on the inside can have a thickness of about 40 to 60 mm when it is new. By regrinding the thickness of the shell can be allowed to be reduced to a value slightly less than 25 mm in order to withstand the internal steam pressure in the cylinder.
Due to the shell surface thickness and the large diameter of the cylinder a Yankee dryer therefore has a considerable mass which must be heated by the steam. The great thickness reduces the heat transfer to the shell surface of the cylinder. Due to this it is difficult to obtain the sufficiently high heat flow required by the drying through the shell surface of a Yankee dryer, and therefore the temperature on the shell surface usually is 95 to 100 °C at the most.
A further problem encountered when the diameter of a Yankee dryer is increased is the difficulty to keep the same temperature on the cylinder shell and the cylinder ends, so that the shape of the cylinder remains constant in the machine cross direction. Temperature differences can result in high tensions between the shell surface and the ends as they are not able to expand freely and independently of each other.
In present day tissue machines the internal surface of a Yankee dryer is usually provided with grooves. Each groove requires an individual outlet for condensate. Therefore the system for conducting condensate out from the cylinder can be highly complicated.
The object of the present invention is to provide a method and a cylinder for heat- ing or cooling a fibrous web where the above-mentioned disadvantages are minimised.
An object is then also to increase the heat transfer capacity in a machine for heating or cooling a fibrous web with a cylinder without essentially increasing the space required for the heat transfer. An object is also to provide a way to increase the heat transfer capacity of drying cylinders without necessarily increasing the size of the cylinder or without using additional energy in order to heat the shell surface of the cylinder.
An object is also to use a heat transfer liquid instead of steam. It is essential that the heat transfer medium remains in liquid form during the entire heat transfer process. An object is also that the heat emission is based on heat energy, which the liquid emits when cooling. An object is also to use a closed system whereby the pressure in the piping system is close to the atmospheric pressure, and to use a liquid having a boiling point clearly above 100 °C, typically at least near 400 °C or even higher.
The above-mentioned objects are attained by a method and a cylinder being characterized by what is presented in the characterizing part of the enclosed independent claims.
In a typical method according to the invention for heating, drying or cooling a fi- brous web, in the making or treating of a fibrous web in a machine having at least one cylinder, which heats or cools the fibrous web, in which cylinder the wall is made of metal or some other suitable heat transferring material, whereby the fibrous web is guided over the heating or cooling cylinder in a heat transfer contact with at least a part of the shell surface of the cylinder, whereby the medium heat- ing or cooling the shell surface of the cylinder is a heat transfer liquid, such as heat transfer oil or the like which remains in liquid form during the heat transfer process. The steam pressure of the liquid is less than 80 kPa within the temperature range that is relevant for the implementation of the method. Thereby the initial boiling point is typically above the upper limit of this temperature range.
The medium heating or cooling the shell surface of the cylinder is conducted through the cylinder in passages in direct or indirect heat transfer contact with the cylinder wall.
A typical cylinder for the heating or cooling a fibrous web in a machine for the making or treating of the fibrous web comprises a cylinder wall of metal or some other suitable material which transfers heat, end walls, and passages for conducting a heat emitting or heat receiving medium through the cylinder. The passages for conducting the heat emitting or heat receiving medium through the cylinder are typically passages formed in the material of the cylinder wall, or passages arranged at or in the cylinder wall, in order to conduct the medium heating or cooling the shell surface of the cylinder through the cylinder in direct or indirect heat transfer contact with the cylinder wall. The heat emitting or receiving heat transfer medium comprises a heat transfer liquid, such as heat transfer oil or the like, which remains in liquid form during the heat transfer process. The steam pressure of the liquid is less than 80 kPa within the temperature range that is relevant for the implementation of the heat transfer between the heat transfer liquid and the cylinder. The initial boiling point of the heat transfer liquid is thereby typically above the upper limit of this temperature range.
In tissue machines are thereby utilized advantageously heat transfer liquids having an initial boiling point above 250 °C, suitably above 300 °C, preferably above 350 °C, and having preferably a vapour pressure lower than 10 kPa at 300 °C.
In one embodiment of the invention heat transfer oils with a temperature > 100 °C, typically 150 to 300 °C, can be suitably used as the heat transfer medium in drying cylinders.
However, in most cases the use of heat transfer oils as heat transfer medium in drying cylinders requires some slight modifications in the actual cylinder construction. Different constructions are conceivable.
Heat transfer oil could be sprayed on the inner surface of the cylinder and removed from the cylinder in a suitable way, e.g. with a siphon, in a similar way as water- steam condensate is removed from conventional drying cylinders with the aid of a pressure difference. The heat exchange oil could be removed out of the cylinder by designing the cylinder as a pressure vessel, or with a pump and a suction pipe. In order to make the heat transfer more effective the inner surface of the cylinder can be provided with radial or axial grooves or grooves in the direction of the shell pe- riphery.
A more effective heat transfer is obtained if the heat transfer oil is conducted through tubes, heat exchanger tubes, which are in contact with the inner surface of the cylinder wall. This practice requires a good heat transfer contact between the heat exchanger tubes and the cylinder wall. A good contact can be obtained by fill- ing the space between the heat exchanger tubes and the cylinder wall with some material having good heat transfer characteristics. One could for example hot galvanize with zinc, so that the spaces between the tubes and the wall are filled with zinc. Also other metals or filling materials which provide a good heat transfer contact between tubes and cylinder wall could be used. Instead of the separate heat exchanger tubes, axial grooves shaped in the inner wall of the cylinder can provide the passages for the heat transfer oil. The grooves can be covered by an additional inner cylindrical plate or inner wall so that separate passages are formed in the wall of the cylinder. It is also possible to shape separate passages in the actual wall material, e.g. by drilling passages in it.
According to a typical embodiment of the invention the passages formed in the cylinder wall, or those passages arranged at or in the cylinder wall, are mainly in parallel with the cylinder axis, and all of them are arranged separately or in groups at an equal distance from the cylinder axis. The diameter of the passages formed in the cylinder wall or the passages arranged at or in the cylinder wall can be mainly constant in the direction of the cylinder axis, but on the other hand the diameter can be, if so desired, e.g. increasing in the flow direction in order to maintain a constant heat transfer from the heat transfer oil or the like to the shell surface of the cylinder, despite the temperature change in the flow direction. On the other hand it is also possible to maintain a constant heat transfer from the heat transfer medium to the shell surface by arranging the passages with a constant diameter at a distance from the shell surface, which distance decreases in the flow direction of the passages. An even heat transfer in the axial direction of the cylinder can also be obtained when every second passage is arranged to convey the heat transfer oil or the like from the tender side to the drive side of the machine and every second passage is arranged to transfer the heat transfer oil or the like from the drive side to the tender side.
According to a typical embodiment of the present invention heat transfer oil or other suitable heat transfer material is supplied into a drying cylinder through an inlet at one axle journal of the cylinder, and distributed from it via a manifold arranged at the inner wall of the cylinder, for example on the drive side of the cylinder, to passages formed in the cylinder wall or to heat exchanger tubes arranged at or in the cylinder wall. In a corresponding way the inner wall of the cylinder on the tender side can be provided with a collector which collects the heat transfer oil or the like from the heat exchanger tubes or passages in order to be drained through an outlet arranged in the other axle journal.
In order to obtain in a cylinder according to the invention an even heat transfer in the axial direction over the entire cylinder surface, the heat transfer medium should not be cooled or heated too much as it flows through the cylinder. In a drying cylinder according to the invention the heat transfer medium can be suitably cooled about 10 °C as it flows through the cylinder. The cooling of the heat transfer medium can be compensated for by making the cylinder wall slightly conical, so that the walls at the inlet side are for instance 10 % thicker than at the outlet side, which will compensate for the temperature change between the inlet and outlet sides. Another alternative way to compensate for the temperature changes is to allow the heat transfer medium to flow in a first direction in every second heat exchanger tube and in the opposite direction in the other tubes.
The invention is described in more detail below with reference to the following drawings:
Figure 1 shows a schematic cross section through a part of a cylinder's cylinder wall according to the invention,
Figure 2 shows a schematic cross section through a part of another cylinder's cylinder wall according to the invention,
Figure 3 shows schematically an axial cross section of a cylinder according to the invention, and
Figure 4 shows a schematic flow diagram for the heat transfer medium between a drying cylinder and an apparatus for heating the heat transfer medium.
In figure 1 is shown a cross section of a sector of the cylinder wall 10 in a drying cylinder. A number of heat exchanger tubes 14 are arranged in the cylinder wall at its inner side 12. The tubes 14 are arranged in parallel with the cylinder axis and at an equal distance from the axis. The tubes 14 are fastened to the inner side 12 of the cylinder wall with the aid of hot galvanizing with zinc 16, which partly encircles the tubes and fills the space between the tubes and the inner side of the cylin- der wall. The galvanizing with zinc provides a good heat transfer contact between the tubes and the inner side of the cylinder wall.
Hot heat transfer oil is arranged to flow through the tubes, whereby heat is transferred from the oil via the tube wall, the zinc layer and the cylinder wall to the shell surface 18 of the cylinder, in order to heat that fibrous web which is to be dried by the drying cylinder.
In figure 1 is shown an advantageous embodiment of the invention in heating and drying of a fibrous web, such as a soft paper web, according to which the heat emitting, heating and drying medium is conducted through the drying cylinder in heat transferring contact with the cylinder wall through heat exchanger tubes arranged at the inner surface of the cylinder wall or in the cylinder wall. A good heat transfer contact between the heat exchanger tubes and the cylinder wall is obtained by adding material with good heat transfer characteristics between the cylinder wall and the tubes arranged at its inner surface. The heat exchanger tubes can e.g. be fastened to the cylinder wall by hot galvanizing with zinc.
In figure 2 is shown an alternative embodiment according to the invention for the heating of the shell surface 18 of a drying cylinder. In figure 2 the inner side 12 of the cylinder wall 10 has passages 14 formed in the actual material of the cylinder wall. The passages 14 are covered by a thin inner cylinder 20 forming a wall which closes the passages, so that separate tube-like passages are formed at the inner wall of the drying cylinder, partly embedded in the wall material.
Figure 2 shows an advantageous embodiment of the invention in heating and dry- ing a fibrous web, such as a soft paper web, according to which the heat emitting, heating and drying medium is conducted through the drying cylinder in direct or indirect heat transfer contact with the cylinder wall via passages formed in the material of the cylinder wall.
Figure 3 shows an axial cross section of a drying cylinder 22 according to the invention. An inlet 28 for heat transfer medium m is arranged through a first axle journal 26 at the first end 24 of the drying cylinder, and an outlet 34 for the heat transfer medium is arranged through the second axle journal 32 at the second end 30. The inlet 28 is connected to a manifold 36 arranged at the inner side of the first end. In a corresponding way the outlet 34 is connected to a collector 38 arranged at the inner side of the second end. The manifold 36 and the collector 38 are interconnected by heat exchanger tubes or passages 14, for example of that type shown in figures 1 and 2. Heat transfer liquid, such as heat transfer oil, is arranged to flow at a temperature of > 100 °C, preferably 150 to 300 °C, from the inlet 28 via the manifold 36, the tubes or passages 14, the collector 38 and the outlet 34, through the drying cylinder 22, in order to heat the shell surface 18 of the cylinder.
Figure 4 shows a system for heating the shell surface 18 of a drying cylinder 22. The heat transfer medium is in this case heat transfer oil. 230 kg/s oil at a temperature of 220 °C is supplied into the drying cylinder 22 via an inlet 28. In the drying cylinder the oil flows through tubes or passages 14 and emits heat through the cyl- inder wall to the shell surface 18 of the cylinder, after which the oil flows out from the cylinder via the outlet 34 at a temperature of about 210 °C. The main part of the drained oil, 197 kg/s, is conducted via a circulation line 38, a valve 40 and an inlet line 42 with a pump 44, back to the inlet 28 of the drying cylinder 22. A partial flow, 33 kg/s, of the drained oil is conducted via a line 46 to a heating appara- tus 48, where the oil is heated to a temperature of 280 °C. The heated oil is conducted via a line 50 to the valve 40 in order to be supplied to the inlet line 42 together with the main part of the oil. In the inlet line the partial flow of heated oil is mixed together with the main part of oil, which provides a flow of 230 kg/s oil at a temperature of 220 °C in the inlet line. According to this system only a part of the oil must be circulated through the heating apparatus. The temperature of that oil which is supplied in the drying cylinder can be rapidly adjusted by adjusting, in a way known as such, the ratio between the two oil flows, the main flow and the partial flow. The heat transfer oil remains in liquid form during the heat transfer process.
EXAMPLE
The aim of the following example is to show that with a drying cylinder according to the invention there can be obtained the same or an substantially higher, e.g. 50 % higher, heat transfer rate than with a conventional steam heated drying cylinder.
The following conditions apply in the comparison: - the diameter of the cylinder is 4572 mm and the width of the web is 5000 mm;
- the k-value, steam / shell surface of the cylinder, is assumed to be 0.7 kW/m2/°C for the steam-heated cylinder, at a steam temperature of 170 °C (7 kPa);
- the k-value for the oil-heated cylinder is assumed to be the same;
- the oil-heated cylinder is assumed to be designed so that it emits 50 % more heat than the steam-heated cylinder;
- the temperature of the shell surface of the steam-heated cylinder is 100 °C;
- the temperature of the shell surface of the oil-heated cylinder is 110 °C.
The temperature of the heat transfer oil should be 110 °C + 1.5 x (170 - 100)°C = 215 °C in order to obtain a temperature of 110 °C at the shell surface. Therefore the oil temperature before the cylinder should be 220 °C and after the cylinder 210 °C, which gives an average temperature of 215 °C.
Then the entire cylinder emits heat according the following:
π x 4.572 m x 5.00 m x 0.7 kW/m2/°C x (215 - 110)°C = 5279 kW The specific heat of oil is 2.3 kJ/kg/°C. At 10 °C ΔT the required amount of oil is thereby 230 kg/s, having a volume flow of 252 1/s (density 910 kg/m3).
The outer/inner diameter of the heat exchanger tubes is assumed to be 21/17 mm, and the tube distance at the cylinder wall to be 28 mm. Thus the wall contains 504 tubes in total. Thus the oil flow in the tubes is 2.2 m/s.
At this flow rate the heat transfer coefficient from the oil to the inner wall of the tube is 1.55 kW/m /°C. The thermal conductivity of the wall is assumed to be 50 W/m/°C. A wall thickness of 39 mm from the bottom of the groove to the ex- ternal surface of the cylinder provides the mentioned k-value 0.7 kW/m /°C, which shows that with oil heating it is possible to achieve a corresponding k-value as with steam heating of a cylinder.
The present invention proposes that drying cylinders are heated with heat transfer oil or a corresponding medium instead of steam, which medium does not evaporate at the temperature and pressure in question. Several heat transfer oils of different types, which can be used at temperatures of up to 300 °C and which are suitable for heating purposes in different embodiments of the invention, are available.
As an example of commonly available suitable heat transfer oils can be mentioned as an example Thermia B and Thermia E from Shell. The initial boiling point of Thermia B is about 355 °C, and of Thermia E about 410 °C. In using these oils the temperature of the heat emitting surface should not exceed 340 °C. At 300 °C the steam pressure of Thermia B is hardly 10 kPa, and at 220 °C it is less than 1 kPa. The steam pressure of Thermia E is lower.
With a method according to the invention there can be obtained among other things the following advantages when drying fibrous webs:
- It is not necessary to dimension the drying cylinder as a pressure vessel.
- It is possible to increase the temperature level of the heat emitting medium from the present 160 - 180 °C (for water steam) to almost 300 °C (for heat transfer oil).
- The temperature level can be raised from the present level to a higher temperature level without increasing the size of the actual drying cylinder construction.
The invention can be utilized to increase the drying capacity of large drying cylinders, for example of the Yankee dryer type, having a large diameter > 2 m, usually 3 to 6 m. The invention can be utilized for example in Yankee dryers in tissue machines. The drying capacity of the cylinder can be controlled in a simple manner by adjusting the temperature of the oil. The invention can be utilized as well in large cylinders with a plain surface for the making of e.g. crepe paper, as in large cylinders with a patterned surface for making of structured soft paper.
The invention can also be applied in conventional drying sections in paper machines. The capacity of existing drying sections can be increased by replacing conventional steam-heated cylinders with oil-heated cylinders of the same size.
The invention can also be advantageously utilized in cylinders which cool fibrous webs, whereby the heat transfer medium, in this case the cooling medium, is cold water. The cylinder provides an improved heat transfer effect or a lower water consumption.
The drying cylinders are typically made of metal, such as steel or cast iron.
The present invention should not be limited to apply only to the above-described preferred embodiments, but it is intended to cover also different modifications within the scope of protection defined in the claims.

Claims

Claims
1. A method of heating or cooling a fibrous web in the making or treating of the fibrous web in a machine having at least one cylinder, which heats or cools the fibrous web, in which cylinder the cylinder wall is of metal or other suitable heat transferring material, said method comprising
- guiding the fibrous web over the heating or cooling cylinder in heat transfer contact with at least a part of the shell surface of the cylinder, and
- heating or cooling the shell surface of the cylinder with a heat emitting or heat receiving medium which is conducted through the cylinder in direct or indirect heat transfer contact with the cylinder wall, characterized by
- using as the medium heating or cooling the shell surface of the cylinder a heat transfer liquid, such as heat transfer oil, which remains in liquid form during the heat transfer process and has a steam pressure that is lower than 80 kPa within the temperature range that is relevant to the implementation of the method.
2. A method of heating a fibrous web according to claim 1, characterized by using a heat transfer liquid having an initial boiling point, which is above the upper limit of the temperature range that is relevant to the implementation of the method.
3. A method of heating a fibrous web according to claim 2, characterized by using a heat transfer liquid having an initial boiling point, which is higher than 250
°C, suitably higher than 300 °C, preferably higher than 350 °C.
4. A method of heating a fibrous web according to claim 1 , characterized by using a heat transfer liquid having a steam pressure, which is lower than 10 kPa at 300 °C.
5. A method of heating a fibrous web according to claim 1, characterized by using as the medium heating or cooling the shell surface of the cylinder a heat transfer oil with a temperature of > 100 °C, preferably between 150 °C and 300 °C.
6. A method of heating a fibrous web according to claim 1, characterized by guiding the fibrous web in heat transfer contact over the shell surface of a drying cylinder, such as a Yankee dryer or other drying cylinder, preferably with a large diameter > 2 m and with a plain or patterned shell surface.
7. A method according to claim 1, characterized in that the fibrous web to be heated or cooled is a structured or unstructured soft paper web, a tissue web or other corresponding web of paper.
8. A method according to claim 1, characterized by conducting the heat emit- ting or receiving medium in direct or indirect heat transfer contact with the cylinder wall through passages formed in the material of the cylinder wall.
9. A method according to claim 1, characterized by conducting the heat emitting or receiving medium in heat transfer contact with the cylinder wall through heat exchanger tubes arranged at the inner surface of the cylinder wall.
10. A method according to claim 9, characterized by providing good heat transfer contact between the heat exchanger tubes and the cylinder wall by adding material with good heat transfer characteristics between the cylinder wall and the tubes arranged at its inner surface.
11. A method according to claim 10, characterized by fastening the heat ex- changer tubes to the cylinder wall by hot galvanizing with zinc.
12. A method of heating a fibrous web according to claim 1, characterized by
- guiding the fibrous web in heat transfer contact over the shell surface of a drying cylinder, such as a Yankee dryer or other drying cylinder, preferably with a large diameter > 2 m and with a plain or patterned shell surface, and - conducting the heat emitting or heat receiving medium in direct or indirect heat transfer contact with the cylinder wall through passages formed in the material of the cylinder wall or through heat exchanger tubes arranged at the inner surface of the cylinder wall, which passages or tubes have a good heat transfer contact with the cylinder wall and its shell surface.
13. A cylinder for the heating or cooling of a fibrous web in a machine for the making or treating of the fibrous web, said cylinder comprising
- a cylinder wall of metal or other suitable heat transfer material,
- end walls, and
- passages for conducting a heat emitting or heat receiving medium through the cylinder, characterized in that
- the passages for conducting the heat emitting or heat receiving medium through the cylinder comprise passages formed in the material of the cylinder wall, or pas- sages arranged at or in the cylinder wall, in order to conduct the medium heating or cooling the shell surface of the cylinder through the cylinder in direct or indirect heat transfer contact with the cylinder wall, and that
- the heat emitting or receiving heat transfer medium is a liquid, such as heat trans- fer oil or the like, which remains in liquid form during the heat transfer process, and that the steam pressure of the liquid is lower than 80 kPa within the temperature range that is relevant to the implementation of the method.
14. A method for the heating of a fibrous web according to claim 13, characterized in that the initial boiling point of the heat transfer liquid is above the upper limit of the temperature range that is relevant to the implementation of the method.
15. A method for the heating of a fibrous web according to claim 14, characterized in that the initial boiling point of the heat transfer liquid is higher than 250 °C, suitably higher than 300 °C, preferably higher than 350 °C.
16. A method for the heating of a fibrous web according to claim 13, character- ized in that the vapour pressure of the heat transfer liquid is lower than 10 kPa at
300 °C.
17. A cylinder according to claim 13, characterized in that the heat emitting or heat receiving medium is heat transfer oil with a temperature of > 100 °C, preferably between 150 °C and 300 °C.
18. A cylinder according to claim 13, characterized in that the cylinder is a drying cylinder, such as a Yankee dryer or other large cylinder, with a diameter of at least 2 m, in a Yankee machine, a tissue machine or other corresponding machine for making soft paper or the like.
19. A cylinder according to claim 13, characterized in that the shell surface of the cylinder is plain or patterned.
20. A cylinder according to claim 13, characterized in that the passages formed in the cylinder wall or arranged at or in the cylinder wall are mainly parallel with the cylinder axis and arranged at an equal distance from the cylinder axis.
21. A cylinder according to claim 13, characterized in that the passages ar- ranged at the cylinder wall are heat exchanger tubes arranged at the inner surface of the cylinder wall.
22. A cylinder according to claim 13, characterized in that the diameter of the passages formed in the cylinder wall or arranged at or in the cylinder wall is mainly constant in the direction of the cylinder axis.
23. A cylinder according to claim 13, characterized in that the diameter of the passages formed in the cylinder wall or arranged at or in the cylinder wall increases in the flow direction in order to maintain a constant heat transfer from the heat transfer oil or the like to the shell surface of the cylinder, despite the temperature change in the flow direction.
24. A cylinder according to claim 13, characterized in that the passages formed in the cylinder wall in the cylinder wall material or arranged at or in the cylinder wall have a constant diameter and that they are arranged at a distance from the shell surface, which distance decreases in the flow direction of the passages in order to maintain a constant heat transfer from the heat transfer oil or the like to the shell surface of the cylinder, despite the temperature change in the flow direction.
25. A cylinder according to claim 13, characterized in that every second passage is arranged to conduct the heat transfer oil or the like from the tender side to the drive side of the machine and that every second passage is arranged to transfer the heat transfer oil or the like from the drive side to the tender side.
26. A cylinder according to claim 13, characterized in that a good heat transfer contact between the passages arranged at the inner wall of the cylinder and the cylinder wall is provided by adding material with good heat transfer characteristics between the cylinder wall and the passages, for instance by hot galvanizing with zinc.
PCT/FI2002/000447 2001-05-23 2002-05-23 Method and cylinder for heating or cooling of a fibrous web WO2002095125A1 (en)

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FI20011077A FI110703B (en) 2001-05-23 2001-05-23 Method and cylinder for heating or cooling a fibrous web
FI20011077 2001-05-23

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WO2006072507A1 (en) * 2005-01-05 2006-07-13 Voith Patent Gmbh Dry cylinder
WO2006072505A1 (en) 2005-01-05 2006-07-13 Voith Patent Gmbh Device and method for producing and/or transforming a web of fibrous material
DE102012104464A1 (en) * 2012-05-23 2013-11-28 Gapcon Gmbh Temperable cylinder for the treatment of flat materials
US10094067B2 (en) * 2016-04-11 2018-10-09 Valmet Technologies, Inc. Production line for producing fiber webs and a cooler
CN112176769A (en) * 2020-10-14 2021-01-05 智君(大连)科技发展有限公司 Rust-resistant paper processing coating drying device

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Publication number Priority date Publication date Assignee Title
CN112695558B (en) * 2021-01-27 2023-06-02 轻工业杭州机电设计研究院有限公司 Heat conduction oil dryer structure

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US6158501A (en) * 1993-10-20 2000-12-12 Valmet Corporation Thermally insulated roll and insulation assembly for a thermoroll

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US4146972A (en) * 1975-10-15 1979-04-03 Smitherm Industries, Inc. Continuous web drying
US5549154A (en) * 1992-02-24 1996-08-27 Valmet Corporation Method for heating a roll and a heatable roll
US6158501A (en) * 1993-10-20 2000-12-12 Valmet Corporation Thermally insulated roll and insulation assembly for a thermoroll
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Publication number Priority date Publication date Assignee Title
WO2006072507A1 (en) * 2005-01-05 2006-07-13 Voith Patent Gmbh Dry cylinder
WO2006072505A1 (en) 2005-01-05 2006-07-13 Voith Patent Gmbh Device and method for producing and/or transforming a web of fibrous material
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CN112176769A (en) * 2020-10-14 2021-01-05 智君(大连)科技发展有限公司 Rust-resistant paper processing coating drying device

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FI20011077A (en) 2002-11-24
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