WO2006128963A2 - Method and arrangement for exhausting gas from a coating material - Google Patents

Method and arrangement for exhausting gas from a coating material Download PDF

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Publication number
WO2006128963A2
WO2006128963A2 PCT/FI2006/050203 FI2006050203W WO2006128963A2 WO 2006128963 A2 WO2006128963 A2 WO 2006128963A2 FI 2006050203 W FI2006050203 W FI 2006050203W WO 2006128963 A2 WO2006128963 A2 WO 2006128963A2
Authority
WO
WIPO (PCT)
Prior art keywords
coating material
drum
tank
step levels
kpa
Prior art date
Application number
PCT/FI2006/050203
Other languages
French (fr)
Other versions
WO2006128963A3 (en
Inventor
Heikki Vatanen
Timo Nurmiainen
Jukka Koskinen
Ilpo Honkanen
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.
Priority to US11/915,973 priority Critical patent/US7935179B2/en
Priority to EP06725960.6A priority patent/EP1885467B1/en
Priority to CN2006800156206A priority patent/CN101171065B/en
Priority to JP2008514134A priority patent/JP5107238B2/en
Publication of WO2006128963A2 publication Critical patent/WO2006128963A2/en
Publication of WO2006128963A3 publication Critical patent/WO2006128963A3/en

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Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/78—Controlling or regulating not limited to any particular process or apparatus
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H19/00—Coated paper; Coating material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0021—Degasification of liquids by bringing the liquid in a thin layer
    • B01D19/0026—Degasification of liquids by bringing the liquid in a thin layer in rotating vessels or in vessels containing movable parts

Definitions

  • the invention relates to a method and arrangement for exhausting gas from a coating material.
  • the coating material is fed in the bottom part area of a drum rotating around an essentially vertical axis, whereby the rotating motion of the drum causes the coating material to rise up the inner wall of the drum and to discharge from the upper edge of the drum as a thin film against the inner wall of a vacuum tank, wherefrom the coating material flows downwards.
  • the apparatus comprises a tank, including means for providing a vacuum in the tank, a drum arranged inside the tank to rotate around a vertical axis, means for feeding coating material inside the drum, and means for discharging the coating material from the tank.
  • the mixing of gases, such as air, with the liquids and compounds used in the process typically causes many problems.
  • gases such as air
  • the gas and gas bubbles present in the coating material cause unevenness on the surface of the paper, and even areas completely lacking coating.
  • the problem is greater than with others, but the problem is emphasized especially with coating materials which bind more gases than others.
  • coating materials containing talcum typically contain a lot of gas due to the properties of talcum.
  • the significance of the problem depends on the coating process used.
  • the gas content of the coating material may not be higher than 0 - 0.25 percent by volume. Otherwise the gas bound in the coating may cause uncoated spots in the material to be coated, such as paper or board.
  • the device comprises a rotating drum arranged inside a vacuum tank, inside which the coating material is conducted, whereupon due to the centrifugal force, the coating material rises up the inner wall of the drum and discharges from the drum as a thin film colliding with the wall of the vacuum tank.
  • the aim of the method and arrangement according to the present invention is to provide an improved solution for vacuum-operated gas separation by means of which gas contained in coating material can be exhausted better than before.
  • the method according to the invention is characterised in that in the method, the coating material is arranged to rise stepwise up the wall of the drum, so that the coating material will form a thin veil-like film on at least two different step levels, whereupon the gas bubbles in the coating material will break and discharge from the coating material.
  • the apparatus according to the invention is, in turn, characterised in that the inner surface of the drum is designed to be stepped, comprising at least two step levels so that the coating material rising upwards due to the effect of the rotating motion will form a thin veil- like film on the said at least two step levels, respectively.
  • an absolute pressure of about 1 kPa - 15 kPa is provided in the vacuum tank. If the absolute pressure provided in the tank is lower, then, for instance, the evaporating point of the solvent contained in the coating material falls, and there is a risk that the quality of the coating material will deteriorate as a result of gas exhaustion.
  • the thickness of the final veil-like film discharged from the upper edge of the drum is adjusted so as to be at most as thick as the desired coating layer.
  • the thickness of the film can be controlled, for example, by controlling the speed of rotation of the drum and/or the amount of coating material fed into the drum.
  • the radial distance between the said at least two step levels is preferably within the range from 20 mm to 200 mm, more preferably within the range from 40 mm to 120 mm, and the difference in height between the said at least two step levels is preferably within the range from 20 mm to 150 mm, more preferably within the range from 40 mm to 100 mm.
  • the ratio of the diameter of the drum to its height is preferably within the range from 1:1 to 10:1, more preferably within the range from 1:1 to 5:1.
  • vanes on the outer surface of the drum are preferably arranged vanes by means of which the desired pressure impact can be exerted on the surface of the coating material in the vacuum tank, which will reduce or completely remove any foam forming on the bottom of the tank due to the boiling of the paste under low pressure.
  • the greatest advantage of the method and arrangement relating to the present invention is its efficiency, whereby gas contained in coating material can be rapidly and carefully exhausted from a large amount of coating material.
  • Figure 1 shows diagrammatically a prior art vacuum deaerator
  • Figure 2 shows a diagrammatic view in principle of an apparatus according to the invention
  • Figure 3 shows diagrammatically a further development of the apparatus according to the invention.
  • Figure 1 shows diagrammatically a prior art vacuum device for exhausting gas, typically air, from coating material.
  • the arrangement comprises a sealed vacuum tank 1, inside which is provided a drum 3 rotated by a motor 2.
  • the gas-containing coating material is fed inside the drum via a pipe 4.
  • the tank is connected to a vacuum source 5 by means of a vacuum pipe 6.
  • the coating material rises up the inner wall of the drum due to the effect of centrifugal force and is centrifuged as a thin film tangentially from the upper edge of the drum, colliding with the inner wall of the vacuum tank, on which it flows downwards, discharging from the bottom part of the tank through the outlet 7.
  • the air bubble following the film breaks and the air formed is exhausted through the vacuum pipe, via a deaerator in conjunction with the vacuum source.
  • FIG. 2 shows an implementation of the apparatus according to the invention as a diagrammatic view in principle.
  • the apparatus comprises a rotating drum 3 arranged inside the vacuum tank 1, which is driven by a motor 2.
  • the inner surface of the drum is made so as to be stepped, comprising in the embodiment shown three step levels 10, 11, 12, so that due to the effect of the rotating motion, the upwards rising coating material will form a thin, veil-like film on each of the said step levels, respectively.
  • the paste film is led from the upper edge of the drum to the inner wall of the vacuum tank and along that, further to the bottom part of the tank to be transferred to the target of use through outlet 7.
  • the difference in height between successive step levels is preferably within the range from 20 mm to 150 mm, more preferably within the range from 40 mm to 100 mm.
  • the radial distance between the step levels, that is, the width of the veil formed is preferably within the range from 20 mm to 200 mm, more preferably within the range from 40 mm to 120 mm.
  • the solution according to the invention enhances gas exhaustion from paste and increases capacity.
  • the solution also makes possible monitoring during the process and controlling of the operational parameters on the basis of the monitoring.
  • the operational parameters include the speed of rotation of the drum 3, the vacuum level in the tank 1, the height of the liquid level at the bottom of the tank 1, which is influenced by the feed rate of the paste fed into the drum and the discharge rate of the paste led out of the tank.
  • Multi-step veiling of coating paste enhances air exhaustion, whereby it is possible to apply a higher minimum absolute pressure level than in earlier solutions, thus avoiding deterioration of the paste quality, which might result from the possible evaporation of some of the components in the paste caused by too low a pressure level.
  • FIG. 3 shows a further development of the apparatus according to the invention, where vanes 13 are formed on the outer surface of the drum 3.
  • the vanes are designed in such a way that they will direct the flow of air downwards towards the bottom of the container, whereupon pressure will rise beneath the vanes.
  • the pressure may be increased by increasing the number, size and angle of the vanes and by increasing the rotation speed of the drum.
  • the increase in pressure reduces the pressure above the vanes, thus enhancing air exhaustion, and in addition, the flow of air caused by the vanes furthers the breaking of the gas bubbles in the foam.
  • the vanes must be positioned symmetrically, so that they will not cause an imbalance in the rotating drum.
  • the embodiment of Figure 3 may also be realised in connection with a prior art vacuum exhaust device without the multi-step forming of a veil-like film according to the invention.
  • the solution according to the invention may advantageously be utilised in the curtain coating process, where the coating material is conducted to the curtain coater after gas exhaustion either directly or through one or more intermediate tanks.
  • the intermediate tanks may optionally have their own supplementary gas exhaustion.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Degasification And Air Bubble Elimination (AREA)
  • Coating Apparatus (AREA)

Abstract

The invention relates to a method and apparatus for exhausting gas from a coating material. The coating material is fed in the bottom part area of a drum (3) rotating around an essentially vertical axis inside a vacuum tank (1), whereby the rotating motion of the drum causes the coating material to rise up the inner wall of the drum and to discharge from the upper edge of the drum as a thin film against the inner wall of a vacuum tank, wherefrom the coating material flows downwards. In the method, the coating material is arranged to rise up the wall of the drum stepwise, so that the coating material will form a thin veil-like film on at least two different step levels (10- 12), whereupon the gas bubbles in the coating material will break and be discharged from the coating material.

Description

Method and arrangement for exhausting gas from a coating material
The invention relates to a method and arrangement for exhausting gas from a coating material. In the method, the coating material is fed in the bottom part area of a drum rotating around an essentially vertical axis, whereby the rotating motion of the drum causes the coating material to rise up the inner wall of the drum and to discharge from the upper edge of the drum as a thin film against the inner wall of a vacuum tank, wherefrom the coating material flows downwards. The apparatus comprises a tank, including means for providing a vacuum in the tank, a drum arranged inside the tank to rotate around a vertical axis, means for feeding coating material inside the drum, and means for discharging the coating material from the tank.
In the process industry, the mixing of gases, such as air, with the liquids and compounds used in the process typically causes many problems. Particularly in the coating of paper or a corresponding web material, the gas and gas bubbles present in the coating material cause unevenness on the surface of the paper, and even areas completely lacking coating. With some coating materials, the problem is greater than with others, but the problem is emphasized especially with coating materials which bind more gases than others. For example, coating materials containing talcum typically contain a lot of gas due to the properties of talcum.
In addition, the significance of the problem depends on the coating process used. In curtain coating, for instance, the gas content of the coating material may not be higher than 0 - 0.25 percent by volume. Otherwise the gas bound in the coating may cause uncoated spots in the material to be coated, such as paper or board.
In multilayer curtain coating, the significance of gas exhaustion is increased further. This means that if there are, for instance, three or four coating layers, gas must be exhausted as carefully as possible from the coating used for making each layer.
For exhausting gas mixed with and dissolved in coating material have been developed vacuum deaerators, one known implementation of which is shown in Figure 1. The device comprises a rotating drum arranged inside a vacuum tank, inside which the coating material is conducted, whereupon due to the centrifugal force, the coating material rises up the inner wall of the drum and discharges from the drum as a thin film colliding with the wall of the vacuum tank.
The problem with prior art vacuum deaerators is their insufficient deaeration efficiency, especially with high-viscosity materials. This is because even under an extremely high vacuum, that is, low absolute pressure, the small air bubbles contained in high-viscosity coating materials are unable to grow large enough to be broken or to be distinguished due to their specific rising speed. Attempts have been made to eliminate this problem by increasing the vacuum, but as a result, the solvent used in the coating material evaporates extremely readily, thus deteriorating the quality of the coating material due to, for example, an increase in the solids content of the coating material following the evaporation of the solvent. As another method are used longer mixing periods, but then the functional capacity of the deaerators remains too low, whereby more devices have to be bought. Moreover, if the separating capacity of known deaerators is increased by increasing the size of the devices, the size of the devices will become excessive and manufacturing costs will increase markedly.
The aim of the method and arrangement according to the present invention is to provide an improved solution for vacuum-operated gas separation by means of which gas contained in coating material can be exhausted better than before. To achieve the aims of the invention, the method according to the invention is characterised in that in the method, the coating material is arranged to rise stepwise up the wall of the drum, so that the coating material will form a thin veil-like film on at least two different step levels, whereupon the gas bubbles in the coating material will break and discharge from the coating material. The apparatus according to the invention is, in turn, characterised in that the inner surface of the drum is designed to be stepped, comprising at least two step levels so that the coating material rising upwards due to the effect of the rotating motion will form a thin veil- like film on the said at least two step levels, respectively.
In a preferred embodiment according to the present invention, an absolute pressure of about 1 kPa - 15 kPa is provided in the vacuum tank. If the absolute pressure provided in the tank is lower, then, for instance, the evaporating point of the solvent contained in the coating material falls, and there is a risk that the quality of the coating material will deteriorate as a result of gas exhaustion.
On the other hand, if a higher absolute pressure is provided in the tank, it will not necessarily be sufficient for increasing the size of the gas bubbles by means of a vacuum. In a highly advantageous case, an absolute pressure of about 3 kPa - 15 kPa is provided in the vacuum tank. Increasing the lower limit of the absolute pressure applied ensures even better that the coating material will not be able to evaporate during gas exhaustion.
In the method according to the invention, the thickness of the final veil-like film discharged from the upper edge of the drum is adjusted so as to be at most as thick as the desired coating layer. The thickness of the film can be controlled, for example, by controlling the speed of rotation of the drum and/or the amount of coating material fed into the drum. In the apparatus according to the invention, the radial distance between the said at least two step levels is preferably within the range from 20 mm to 200 mm, more preferably within the range from 40 mm to 120 mm, and the difference in height between the said at least two step levels is preferably within the range from 20 mm to 150 mm, more preferably within the range from 40 mm to 100 mm. The ratio of the diameter of the drum to its height is preferably within the range from 1:1 to 10:1, more preferably within the range from 1:1 to 5:1.
In the apparatus according to the invention, on the outer surface of the drum are preferably arranged vanes by means of which the desired pressure impact can be exerted on the surface of the coating material in the vacuum tank, which will reduce or completely remove any foam forming on the bottom of the tank due to the boiling of the paste under low pressure.
The greatest advantage of the method and arrangement relating to the present invention is its efficiency, whereby gas contained in coating material can be rapidly and carefully exhausted from a large amount of coating material.
The invention is described in greater detail in the following, with reference to the accompanying drawing, in which:
Figure 1 shows diagrammatically a prior art vacuum deaerator,
Figure 2 shows a diagrammatic view in principle of an apparatus according to the invention, and
Figure 3 shows diagrammatically a further development of the apparatus according to the invention. Figure 1 shows diagrammatically a prior art vacuum device for exhausting gas, typically air, from coating material. As shown in the Figure, the arrangement comprises a sealed vacuum tank 1, inside which is provided a drum 3 rotated by a motor 2. The gas-containing coating material is fed inside the drum via a pipe 4. The tank is connected to a vacuum source 5 by means of a vacuum pipe 6. When the drum rotates, the coating material rises up the inner wall of the drum due to the effect of centrifugal force and is centrifuged as a thin film tangentially from the upper edge of the drum, colliding with the inner wall of the vacuum tank, on which it flows downwards, discharging from the bottom part of the tank through the outlet 7. The air bubble following the film breaks and the air formed is exhausted through the vacuum pipe, via a deaerator in conjunction with the vacuum source.
Figure 2 shows an implementation of the apparatus according to the invention as a diagrammatic view in principle. The apparatus comprises a rotating drum 3 arranged inside the vacuum tank 1, which is driven by a motor 2. The inner surface of the drum is made so as to be stepped, comprising in the embodiment shown three step levels 10, 11, 12, so that due to the effect of the rotating motion, the upwards rising coating material will form a thin, veil-like film on each of the said step levels, respectively. Once discharged from the final step, the paste film is led from the upper edge of the drum to the inner wall of the vacuum tank and along that, further to the bottom part of the tank to be transferred to the target of use through outlet 7. In the top part area of the tank 1 are preferably arranged means 20 for imaging the veil-like film, whereby when the veil-like film remains intact, there will be no more air bubbles left in the paste. The image data obtained from the imaging means 20 can be used to control the operational parameters of the degassing device. The step levels may be made, for example, in accordance with Figure 2 of successive concave sections, the front edges 10a, 11a, 12a of which determine the elevation of the step level, that is, the elevation of the thin, veil-like film formed. To achieve efficient gas exhaustion and for compact dimensioning of the apparatus, the difference in height between successive step levels is preferably within the range from 20 mm to 150 mm, more preferably within the range from 40 mm to 100 mm. The radial distance between the step levels, that is, the width of the veil formed is preferably within the range from 20 mm to 200 mm, more preferably within the range from 40 mm to 120 mm.
The solution according to the invention enhances gas exhaustion from paste and increases capacity. The solution also makes possible monitoring during the process and controlling of the operational parameters on the basis of the monitoring. The operational parameters include the speed of rotation of the drum 3, the vacuum level in the tank 1, the height of the liquid level at the bottom of the tank 1, which is influenced by the feed rate of the paste fed into the drum and the discharge rate of the paste led out of the tank.
Multi-step veiling of coating paste enhances air exhaustion, whereby it is possible to apply a higher minimum absolute pressure level than in earlier solutions, thus avoiding deterioration of the paste quality, which might result from the possible evaporation of some of the components in the paste caused by too low a pressure level.
Figure 3 shows a further development of the apparatus according to the invention, where vanes 13 are formed on the outer surface of the drum 3. The vanes are designed in such a way that they will direct the flow of air downwards towards the bottom of the container, whereupon pressure will rise beneath the vanes. The pressure may be increased by increasing the number, size and angle of the vanes and by increasing the rotation speed of the drum. The increase in pressure reduces the pressure above the vanes, thus enhancing air exhaustion, and in addition, the flow of air caused by the vanes furthers the breaking of the gas bubbles in the foam. The vanes must be positioned symmetrically, so that they will not cause an imbalance in the rotating drum. The embodiment of Figure 3 may also be realised in connection with a prior art vacuum exhaust device without the multi-step forming of a veil-like film according to the invention.
The solution according to the invention may advantageously be utilised in the curtain coating process, where the coating material is conducted to the curtain coater after gas exhaustion either directly or through one or more intermediate tanks. The intermediate tanks may optionally have their own supplementary gas exhaustion.

Claims

Claims
1. A method for exhausting gas from a coating material, in which method, the coating material is fed in the bottom part area of a drum (3) rotating around an essentially vertical axis inside a vacuum tank (1), whereby the rotating motion of the drum causes the coating material to rise up the inner wall of the drum and to discharge from the upper edge of the drum as a thin film against the inner wall of a vacuum tank (1), wherefrom the coating material flows downwards, characterised in that in the method, the coating material is arranged to rise up the wall of the drum stepwise, so that the coating material will form a thin veil-like film on at least two different step levels (10, 11, 12), whereupon the gas bubbles in the coating material will break and/or discharge from the coating material to be then conducted out of the tank-
2. A method as claimed in claim 1, characterised in that the radial distance between the said at least two successive step levels (10, 11, 12) is within the range from 20 mm to 200 mm.
3. A method as claimed in claim 2, characterised in that the radial distance between the said at least two successive step levels (10, 11, 12) is within the range from 40 mm to 120 mm.
4. A method as claimed in any of the above claims, characterised in that the difference in height between the said at least two successive step levels
(10, 11, 12) is within the range from 20 mm to 150 mm.
5. A method as claimed in claim 4, characterised in that the difference in height between the said at least two successive step levels (10, 11, 12) is within the range from 40 mm to 100 mm.
6. A method as claimed in any of the above claims, characterised in that the thickness of the final veil-like film discharged from the drum (3) is adjusted to be at most as thick as the desired coating layer.
7. A method as claimed in any of the above claims, characterised in that an absolute pressure of about 1 kPa - 15 kPa is provided in the vacuum tank (I)-
8. A method as claimed in claim 7, characterised in that an absolute pressure of about 3 kPa - 15 kPa is provided in the vacuum tank (1).
9. A method as claimed in any of the above claims, characterised in that after gas exhaustion, the coating material is conducted from the tank (1) to curtain coater.
10. An apparatus for exhausting gas from a coating material, the apparatus comprising:
- a tank (1) to which are connected means (5, 6) for providing an vacuum in the tank, - a drum (3) arranged inside the tank to rotate around a vertical axis,
- means (4) for feeding coating material inside the drum (3), and
- means (7) for discharging the coating material from the tank, characterised in that the inner surface of the drum is designed to be stepped, comprising at least two step levels (10, 11, 12) so that the coating material rising upwards due to the effect of the rotating motion will form a thin veil-like film on the said at least two step levels (10, 11, 12).
11. An apparatus as claimed in claim 10, characterised in that an absolute pressure of about 1 kPa - 15 kPa is provided in the tank (1).
12. An apparatus as claimed in claim 11, characterised in that an absolute pressure of about 3 kPa - 15 kPa is provided in the tank (1).
13. An apparatus as claimed in claim 10, characterised in that the radial distance between the said at least two successive step levels (10, 11, 12) is within the range from 20 mm to 200 mm.
14. An apparatus as claimed in claim 13, characterised in that radial distance between the said at least two successive step levels (10, 11, 12) is within the range from 40 mm to 120 mm.
15. An apparatus as claimed in any of the claims 10-14, characterised in that the difference in height between the said at least two successive step levels (10, 11, 12) is within the range from 20 mm to 150 mm.
16. An apparatus as claimed in claim 15, characterised in that the difference in height between the said at least two successive step levels (10, 11, 12) is within the range from 40 mm to 100 mm.
17. An apparatus as claimed in any of the claims 10-16, characterised in that on the outer surface of the drum (3) are arranged vanes (13) to provide a pressure impact on the surface of the coating material in the vacuum tank (1) while the drum rotates.
PCT/FI2006/050203 2005-06-02 2006-05-22 Method and arrangement for exhausting gas from a coating material WO2006128963A2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US11/915,973 US7935179B2 (en) 2005-06-02 2006-05-22 Method and arrangement for exhausting gas from a coating material
EP06725960.6A EP1885467B1 (en) 2005-06-02 2006-05-22 Method and arrangement for exhausting gas from a coating material
CN2006800156206A CN101171065B (en) 2005-06-02 2006-05-22 Method and arrangement for exhausting gas from a coating material
JP2008514134A JP5107238B2 (en) 2005-06-02 2006-05-22 Coating material degassing method and apparatus

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20055280A FI117602B (en) 2005-06-02 2005-06-02 Method and apparatus for degassing the coating material
FI20055280 2005-06-02

Publications (2)

Publication Number Publication Date
WO2006128963A2 true WO2006128963A2 (en) 2006-12-07
WO2006128963A3 WO2006128963A3 (en) 2007-02-22

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Country Status (6)

Country Link
US (1) US7935179B2 (en)
EP (1) EP1885467B1 (en)
JP (1) JP5107238B2 (en)
CN (1) CN101171065B (en)
FI (1) FI117602B (en)
WO (1) WO2006128963A2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007074211A1 (en) * 2005-12-28 2007-07-05 Metso Paper, Inc. Method and apparatus for degassing coating material
WO2008037843A1 (en) * 2006-09-29 2008-04-03 Metso Paper, Inc. Method of coating a fibrous web with a curtain coater
US20110073812A1 (en) * 2008-06-03 2011-03-31 Koninklijke Philips Electronics N.V. Method and device for de-gassing a liquid-gas-mixture
US7935179B2 (en) 2005-06-02 2011-05-03 Metso Paper, Inc. Method and arrangement for exhausting gas from a coating material
DE202011108135U1 (en) 2011-11-11 2012-02-06 Metso Paper, Inc. Device for venting a coating medium to be applied to a fibrous web

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE907341C (en) * 1938-10-14 1954-03-25 Maico Elektroapp Fabrik G M B fan
WO2010065028A1 (en) * 2008-12-01 2010-06-10 Halliburton Energy Services Hollow cone degassing
FI123403B (en) * 2010-02-02 2013-03-28 Outotec Oyj Method and apparatus for removing gas from solution
JP6008482B2 (en) * 2011-09-15 2016-10-19 株式会社バンテック Gas generator
CN103182200B (en) * 2011-12-30 2014-09-17 绵阳世诺科技有限公司 On-line continuous degassing device
CN104543863B (en) * 2014-12-01 2018-02-27 安徽鑫乐源食品有限公司 A kind of degassing method of high viscosity, high foam taro slurry food material
CN106149441A (en) * 2015-04-23 2016-11-23 中国制浆造纸研究院 A kind of high-efficiency vacuum deaerator
US10035084B2 (en) * 2016-05-05 2018-07-31 Cook and Cook Incorporated De-aeration system and method

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3213592A (en) * 1963-02-21 1965-10-26 Northern Ind Inc Liquid treatment
DE2147124C3 (en) * 1971-09-21 1974-08-22 Rumpf, Hans, Prof. Dr.-Ing., 7500 Karlsruhe Method and device for degassing liquids
IT1029819B (en) * 1974-02-28 1979-03-20 Feres Vaclav SITTILE LAYER VAPORIZER
FR2468410B1 (en) * 1979-10-31 1985-06-21 Saget Pierre CENTRIFUGAL SEPARATION PROCESS AND APPARATUS FOR IMPLEMENTING IT APPLICABLE TO A MIXTURE OF PHASES OF ANY STATE
FR2556981B1 (en) * 1983-12-23 1988-10-14 Creusot Loire DEGASSING DEVICE FOR ELECTROLYSIS INSTALLATION FOR GAS PRODUCTION, PARTICULARLY FOR WATER ELECTROLYSIS INSTALLATION
US4657677A (en) 1985-02-15 1987-04-14 Roubicek Rudolf V Equipment for enhanced mass transfer and control of foaming in chemical and biochemical processes
JPH07120587B2 (en) 1987-01-23 1995-12-20 松下電工株式会社 Magnetic leakage transformer type ballast
JPH038322Y2 (en) * 1987-05-12 1991-02-28
DE69026097T2 (en) * 1990-12-12 1996-10-02 Agfa Gevaert Nv Curtain coater
JP2841923B2 (en) * 1991-06-07 1998-12-24 日本製紙株式会社 Manufacturing method of coated paper for printing
US5591252A (en) * 1991-07-19 1997-01-07 Wilhelm Hedrich Vakuumanlagen Gmbh & Co. Kg Device and method for the continuous degassing of casting resin
US5951877A (en) * 1995-04-18 1999-09-14 Cobe Laboratories, Inc. Particle filter method
CH691995A5 (en) * 1995-09-02 2001-12-31 Vaclav Feres Apparatus for treating liquid products.
US5972171A (en) * 1997-04-08 1999-10-26 Mobil Oil Corporation De-entrainment tray and method of operation
US6689225B2 (en) * 1999-05-21 2004-02-10 Vortex Holding Company Toroidal vortex vacuum cleaner with alternative collection apparatus
FI111873B (en) * 1999-06-03 2003-09-30 Pom Technology Oy Ab Gas separating centrifugal apparatus, process for pumping and separating gas, and process for making paper or board
JP2001009206A (en) * 1999-06-25 2001-01-16 Noritake Co Ltd Multistage defoaming and degasing device
JP4700872B2 (en) * 1999-07-05 2011-06-15 株式会社横田製作所 Pump device
FI112329B (en) * 2000-07-11 2003-11-28 Metso Paper Inc Device for a dehumidifier and method for controlling its function
US6730146B2 (en) * 2002-05-03 2004-05-04 Kem-Tron Technologies, Inc. Drilling fluid degasser
US6726743B2 (en) * 2002-06-18 2004-04-27 3M Innovative Properties Company Electrostatic deaeration method and apparatus
JP4196372B2 (en) 2002-12-04 2008-12-17 株式会社メカ・エンジ Bubble removal device for viscous fluid
JP2004290859A (en) 2003-03-27 2004-10-21 Nippon Paper Industries Co Ltd Method and apparatus for deaerating liquid
FI117602B (en) 2005-06-02 2006-12-15 Metso Paper Inc Method and apparatus for degassing the coating material

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of EP1885467A4 *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7935179B2 (en) 2005-06-02 2011-05-03 Metso Paper, Inc. Method and arrangement for exhausting gas from a coating material
WO2007074211A1 (en) * 2005-12-28 2007-07-05 Metso Paper, Inc. Method and apparatus for degassing coating material
US7879140B2 (en) 2005-12-28 2011-02-01 Metso Paper, Inc. Method and apparatus for degassing coating material
WO2008037843A1 (en) * 2006-09-29 2008-04-03 Metso Paper, Inc. Method of coating a fibrous web with a curtain coater
AT509528B1 (en) * 2006-09-29 2012-08-15 Metso Paper Inc METHOD FOR COATING A FIBERWHEEL WITH A FORWARD COILTER
US20110073812A1 (en) * 2008-06-03 2011-03-31 Koninklijke Philips Electronics N.V. Method and device for de-gassing a liquid-gas-mixture
DE202011108135U1 (en) 2011-11-11 2012-02-06 Metso Paper, Inc. Device for venting a coating medium to be applied to a fibrous web
AT13518U1 (en) * 2011-11-11 2014-02-15 Metso Paper Inc Apparatus for venting a coating medium to be applied to a fibrous web

Also Published As

Publication number Publication date
US7935179B2 (en) 2011-05-03
FI117602B (en) 2006-12-15
US20080166488A1 (en) 2008-07-10
FI20055280A0 (en) 2005-06-02
EP1885467B1 (en) 2020-02-19
CN101171065B (en) 2010-08-11
WO2006128963A3 (en) 2007-02-22
CN101171065A (en) 2008-04-30
EP1885467A2 (en) 2008-02-13
JP5107238B2 (en) 2012-12-26
EP1885467A4 (en) 2012-01-18
JP2008542012A (en) 2008-11-27

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