EP2739923A1 - Verfahren und vorrichtung zur trocknung eines auf ein substrat aufgetragenen fluidfilms - Google Patents
Verfahren und vorrichtung zur trocknung eines auf ein substrat aufgetragenen fluidfilmsInfo
- Publication number
- EP2739923A1 EP2739923A1 EP12741294.8A EP12741294A EP2739923A1 EP 2739923 A1 EP2739923 A1 EP 2739923A1 EP 12741294 A EP12741294 A EP 12741294A EP 2739923 A1 EP2739923 A1 EP 2739923A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- temperature
- heat source
- transport
- substrate
- fluid film
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 239000012530 fluid Substances 0.000 title claims abstract description 50
- 239000000758 substrate Substances 0.000 title claims abstract description 47
- 238000001035 drying Methods 0.000 title claims abstract description 46
- 238000000034 method Methods 0.000 title claims abstract description 30
- 238000010438 heat treatment Methods 0.000 claims abstract description 45
- 239000007788 liquid Substances 0.000 claims abstract description 43
- 230000008016 vaporization Effects 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims description 26
- 238000001704 evaporation Methods 0.000 claims description 7
- 230000008020 evaporation Effects 0.000 claims description 6
- 230000001105 regulatory effect Effects 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
- 230000001276 controlling effect Effects 0.000 claims description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 2
- 239000001569 carbon dioxide Substances 0.000 claims description 2
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 claims description 2
- 230000008569 process Effects 0.000 claims description 2
- 230000004044 response Effects 0.000 claims description 2
- 238000005485 electric heating Methods 0.000 claims 1
- 238000011010 flushing procedure Methods 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 239000010408 film Substances 0.000 description 39
- 238000009792 diffusion process Methods 0.000 description 12
- 238000011144 upstream manufacturing Methods 0.000 description 8
- 238000004140 cleaning Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 101100346656 Drosophila melanogaster strat gene Proteins 0.000 description 1
- 235000010678 Paulownia tomentosa Nutrition 0.000 description 1
- 240000002834 Paulownia tomentosa Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000005253 cladding Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/18—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
- F26B13/10—Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D3/00—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
- F26B13/06—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement with movement in a sinuous or zig-zag path
- F26B13/08—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement with movement in a sinuous or zig-zag path using rollers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/18—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact
- F26B3/20—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact the heat source being a heated surface, e.g. a moving belt or conveyor
Definitions
- the invention relates to a method and an apparatus for drying a fluid film applied to a substrate which contains a vaporizable liquid.
- the web-shaped goods may be, for example, paper, plastic films, textiles or metal strips.
- a fluid film is applied, which is a
- the object of the invention is to eliminate the disadvantages of the prior art.
- a method and a device are to be specified with which a fluid film applied to a substrate can be dried while avoiding mottling phenomena and with improved efficiency, without having to move large amounts of air.
- This object is solved by the features of claims 1 and 16.
- Advantageous embodiments of the invention will become apparent from the features of claims 2 to 15 and 17 to 26.
- Discharging the vaporized liquid by creating a flow directed from the fluid film towards the heat source.
- the liquid is substantially evaporated by means of a heat source provided opposite the substrate. This eliminates the effort to heat the drying gas. The further effort for cleaning or regeneration of the drying gas can be significantly reduced.
- drying rates of up to 20 g / m 2 s can be achieved. This corresponds to about 10 times those drying rates, which are achieved by the methods known in the prior art.
- the heating surface of the heat source is arranged in a further departure from the prior art only at a distance of 0.1 mm to 15.0 mm, preferably 0.2 to 5.0 mm, opposite the substrate surface, the heat in the inventions ⁇ to the invention Method essentially supplied by direct heat conduction to the fluid film.
- the fluid film facing the heating surface of its boundary surface from being heated in the direction of Substratoberflä ⁇ surface.
- a particularly effec ⁇ tive evaporation or diffusion of the liquid can be achieved.
- the vaporized liquid is removed in the direction of the heat source by the applied temperature gradient. Ie. the evaporated liquid flows Wesentli ⁇ chen perpendicular from the interface, and then passes into egg nen by the boundary surface and the heating surface formed Ka ⁇ nal. It is largely avoided within the fluid film, the generation of a substantially parallel to the interface directed flow with high amounts of air. As a result, no mottling phenomena occur in the fluid film in the method according to the invention.
- a gas flow is generated in the ge ⁇ formed between the heating surface and the interface channel for discharging the evaporated liquid opposite to the transport direction of the substrate.
- the gas flow may be generated, for example, by a suction device which is provided at the upstream end of the channel.
- the evaporated liquid is moved in the direction of each upstream upstream heat source.
- a Strömungsgeschwindig ⁇ ness of the guided in the opposite direction to the transport direction of the substrate flow of gas is preferably 2 cm / s to 30 m / s, preferably 10 cm / s to 10 m / s.
- the Strömungsgeschwin ⁇ speed of the gas depends on the length of the channel and the quantitative ge of liquid to be evaporated. If the evapora- to ⁇ Fende liquid is flammable, should be selected as a gas, an inert gas.
- a first temperature-temperature T G is controlled as a function of the heating surface in an interfacial ⁇ temperature Ti of the fluid film.
- the first temperature T G is adjusted so that the required Abtrans ⁇ port of the liberated fluid vapor from the surface ge is ensured.
- the heat is advantageously transferred from the heating surface to the fluid film essentially by direct heat conduction.
- the first temperature T G is suitably controlled in the range of 50 ° C to 300 ° C, preferably in the range of 80 ° C and 200 ° C.
- the transport surface is heated by means of a further heat source.
- a generated by the heat source further second temperature T H of the transport surface is advantageously regulated depending ⁇ ness of the interface temperature ⁇ .
- the second temperature T H can be regulated in particular such that the following relationship is fulfilled:
- the transport surface is heated to a second temperature T H ⁇ structure by means of a wide ⁇ ren heat source.
- the second temperature T H is set so that it is greater than the interface temperature Ti.
- a particularly large mass flow of the evaporated liquid is advantageously achieved when the Dif ⁇ difference ⁇ between the interface temperature ⁇ and the second temperature T H is in the range of 2 ° C to 30 ° C.
- the evaporation of the liquid egg in ⁇ ner non-combustible gas atmosphere, preferably nitrogen or carbon dioxide atmosphere ⁇ performed. This allows safe and reliable to avoid the ignition of vaporized within the trock ⁇ voltage device flammable liquid.
- the heating surface facing the substrate is at a distance from
- a thickness of the fluid film issverapt ⁇ Lich selected so that it is smaller than the aforesaid distance.
- the fluid film may have a thickness in the range of 5 ym to 200 ym, preferably 10 ym to 50 ym.
- the second temperature T H is controlled so that it is always smaller than the first temperature T G.
- a temperature difference between the first and the second temperature T G T H can in particular be regulated so that along the conveying device ⁇ a predetermined temperature difference profile provides a ⁇ .
- the temperature gradient or the temperature difference between the first T G and the second temperature T H can change along the transport direction in a predetermined manner. This takes into account the fact that the amount of liquid to be evaporated decreases in the transport direction.
- the change of the temperature gradient can be achieved by suitable regulation of the first T G and / or second temperature T H or also be effected by changing the distance of the heating surface from the interface.
- a flow-through heat source is used as the heat source, and the vaporized liquid is performed by the heat source to pass from ⁇ .
- the evaporated liquid in ⁇ We sentlichen can be discharged vertically from the surface of the fluid film and the interface.
- a heat source is suitably an electrical heating ⁇ source, preferably a heating source equipped with resistance heating wires used. In this case can for example be arranged lattice-like, the resistance heating ⁇ wires.
- a heat exchanger may be designed to be flowed through like a radiator for motor vehicles. It is also possible to provide a plurality of heat exchangers in succession in the transport direction, it being possible for a gap to be provided between the heat exchangers in each case. Through the gap, the vaporized liquid can be removed from the surface of the fluid film.
- At least one rotatable roller is used as a transport device, whose lateral surface forms the transport surface.
- the heat source is configured corresponding to the lateral surface of the roller, that is, a heating surface of the heat source is at a predetermined small distance from the Mantelflä- arranged.
- the further heat source is arranged inside the roller.
- the transport surface is heated by an underside of the transport device opposite the substrate, preferably by means of direct heat conduction.
- the transport surface can be electrically heated by means of resistance heating elements.
- Such an electric heater allows a particularly simple control of the temperature of the trans ⁇ port surface.
- an apparatus for drying a fluid film containing a vaporizable liquid applied to a substrate surface comprising: a transport device for transporting the substrate on a transport surface along a transport direction, a heat source provided with a heating surface opposite the substrate; which is located at a distance of 0.1 mm to 15.0 mm opposite to the substrate surface, and means for generating a directed from the fluid film in the direction of the heat source flow.
- the proposed device enables efficient drying of a fluid film applied to a substrate.
- the liquid is evaporated by a heat source provided opposite the substrate.
- the heat source is in departure from the prior art only at a distance of 0.1 to 15.0 mm, preferably 0.1 to 5.0 mm, arranged from the substrate surface.
- the evaporated liquid is dissipated by generating a directed from the substrate in the direction of the heat source flow.
- a device for discharging the evaporated liquid is provided.
- a further heat source for heating the transport surface is provided.
- the further heat source is suitably provided at a tung the sub ⁇ strat opposite "bottom" of the Transportvorrich-. It may be, for example, a resistance heater.
- a first control means for controlling a testified to the heating surface ER- first temperature T G is provided in response to a Grenzflä ⁇ chentemperatur Ti of the fluid film.
- the controlled variable namely, the first temperature T G of the heating surface is Bennett- according to a predetermined algorithm in dependence of the Grenzflä ⁇ chentemperatur Ti which constitutes the command variable represents.
- the first temperature T G can for example be controlled so that a predetermined temperature gradient is formed between the boundary surface tempera ture ⁇ Ti and the first temperature T G.
- a second control device is advantageously provided for controlling a second temperature T H of the transport surface as a function of the interface temperature ⁇ . In this case, the interface temperature ⁇ is measured as a reference variable. Depending on the measured interface temperature ⁇ is the second by means of the control device
- Temperature T H set or tracked.
- the adjustment or the tracking of the second temperature T H occurs expediently such that a predetermined interface temperature ⁇ Ti is kept substantially constant.
- the first T G and the second temperature T H can be measured, for example, by means of conventional thermocouples.
- the interface temperature ⁇ can contactlessly be detected by means of an infrared measuring device Example ⁇ example.
- the first control device can also be omitted.
- the first temperature T G is kept constant.
- the first and second control means may also be gekop ⁇ pelt.
- a temperature gradient between the first T G and the second temperature T H can be regulated in accordance with a further predetermined algorithm so that along the transport direction a predetermined temperature difference profile is established between the transport surface and the heating surface.
- FIG. 3 shows the interface temperature over the transport surface temperature at a given gas temperature
- 4 shows the mass diffusion rate over the gas temperature at a predetermined transport surface temperature
- FIG. 5 shows the mass diffusion rate over the transport surface temperature at a given gas temperature
- Fig. 8 is a schematic sectional view through an exemplary embodiment of an inventive diffusion ⁇ dryer
- FIG. 9 shows a schematic detail view according to FIG. 8 and FIG. 10 shows a schematic sectional view through a further one
- Embodiment of a Diffu ⁇ sionstrockners invention Embodiment of a Diffu ⁇ sionstrockners invention.
- the interface temperature Tj ie the temperature at the free surface of the fluid film
- the mass diffusion rate per unit area based on the temperature gradient at the free surface can be calculated as follows:
- the drying time for the material to be coated can be calculated as follows:
- a L 0.6 W / (mK)
- p L 1000 kg / m 3
- a / i iH 2260 KJ / kg
- the drying of the fluid film according to the invention is determined in Wesent ⁇ union by a control of the second temperature T H to the conveying surface and by the first temperature T G of the heat source.
- the heat source is at a distance ⁇ G of the gas phase facing interface of the fluid film ⁇ introduced .
- FIG. 2 shows the interface temperature T j above the first temperature T G of the heat source or gas phase.
- 3 shows the interface temperature T j above the temperature T H of the transport surface.
- the mass diffusion rate can be achieved by increasing the first temperature Tem ⁇ T G. It can also be seen that an increase in the second temperature T H causes a reduction in the mass diffusion rate. As can be seen in particular from FIGS. 6 and 7, a reduction of the drying time can be achieved if the second temperature T H is small and the first temperature T G is selected to be high. Both temperatures T G and T H are adjustable so that T ⁇ can be controlled. T j can z. B. be kept at room temperature.
- Fig. 8 shows a schematic sectional view of an exporting ⁇ approximately example of a diffusion dryer according to the invention.
- a housing 1 In a housing 1 is a supply roller 2, on which the substrate 3 to be coated is received. The substrate 3 is guided over first tension rollers 4a, 4b on a transport roller 5.
- a cladding or transport surface 6 of the transport roller 5 is ⁇ sections, preferably surrounded over an angle of 180-270 °, by a drying device. 7
- a slot nozzle tool designated by the reference numeral 8 is provided for applying a fluid film F to the substrate 3.
- the drying device 7 is situated at least one further tension roller 9, over which the substrate is wound onto a roll 10.
- Reference numeral 11 designates a roller cleaning device, which is arranged downstream of the drying device 7 and upstream of the coating tool 8.
- the drying device 7 has a further housing 12.
- the further housing 12 is provided with suction devices 14, with which a liquid vapor escaping from the fluid film F is extracted.
- a heat source 13 accommodated in the further housing 12 can be formed, for example, from resistance heating wires, which are arranged like a lattice.
- the heating wires form one Heating surface G, which is arranged at a distance 6 G, for example, 0.1 mm to 1.0 mm opposite the interface I of the fluid film F. 9, a substantially perpendicular to the transport surface 6 forming flow, which is indicated in Fig. 9 by arrows.
- a negative pressure in the space between the interface I and the heating surface H is advantageously generated. This avoids the escape of any combustible liquid vapors into the environment.
- the housing 1 can also be flushed with a protective gas atmosphere in order to avoid a risk of fire or explosion due to the escape of the combustible liquid vapors.
- the apparatus shown in Fig. 8 according to the invention is constructed be ⁇ Sonders compact. Instead of a transport roller 5, a plurality of transport rollers 5 can be used. Thus, a drying section can be increased, which is a
- the device according to the invention can also be used in combination with conventional convection dryers.
- the device according to the invention is expediently used upstream of a conventional convection dryer.
- FIG. 10 Shown in the embodiment shown in FIG. 10 schematic sectional view through a further embodiment of an inventive ⁇ SEN diffusion dryer and a further drying device 15.
- the substrate 3 is in turn received on a supply roll 2; it is done with an Benen roller 16 transported.
- the reference numeral 8 again denotes a slot nozzle tool for applying a fluid film to the substrate 3, which is arranged upstream of a further drying device 15.
- the further drying device 15 comprises in transport ⁇ direction T heating elements 17, which may be in the transport direction T successively arranged plate-shaped resistance heating.
- the heating elements 17 form a substantially closed heating surface H which is arranged at a distance ⁇ G of 2 to 10 mm from a substrate surface.
- the further drying device 15 thus has a rectangular channel K with the height ⁇ G , through which the substrate 3 is guided in the transport direction T.
- a flow rate is for example 30 cm / s to 3 m / s.
- a further transport surface 18 of the further drying device 15 is embodied here. It can also be configured ⁇ heated (not shown here). Reference sign list
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Textile Engineering (AREA)
- Drying Of Solid Materials (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE201110080222 DE102011080222A1 (de) | 2011-08-01 | 2011-08-01 | Verfahren und Vorrichtung zur Trocknung eines auf ein Substrat aufgetragenen Fluidfilms |
DE102012210431 | 2012-06-20 | ||
PCT/EP2012/064305 WO2013017441A1 (de) | 2011-08-01 | 2012-07-20 | Verfahren und vorrichtung zur trocknung eines auf ein substrat aufgetragenen fluidfilms |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2739923A1 true EP2739923A1 (de) | 2014-06-11 |
EP2739923B1 EP2739923B1 (de) | 2016-06-29 |
Family
ID=46601782
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP12741294.8A Active EP2739923B1 (de) | 2011-08-01 | 2012-07-20 | Verfahren und vorrichtung zur trocknung eines auf ein substrat aufgetragenen fluidfilms |
Country Status (10)
Country | Link |
---|---|
US (1) | US9851144B2 (de) |
EP (1) | EP2739923B1 (de) |
JP (1) | JP2014527148A (de) |
KR (1) | KR20140068039A (de) |
CN (1) | CN103814266B (de) |
BR (1) | BR112014002515A2 (de) |
CA (1) | CA2843492A1 (de) |
PL (1) | PL2739923T3 (de) |
RU (1) | RU2647192C2 (de) |
WO (1) | WO2013017441A1 (de) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB201411483D0 (en) * | 2014-06-27 | 2014-08-13 | Batmark Ltd | Vaporizer Assembly |
DE102017128397A1 (de) | 2017-11-30 | 2019-06-06 | Mitsubishi Hitec Paper Europe Gmbh | Verfahren und Vorrichtung zum Herstellen eines beschichteten Substrats sowie beschichtetes Substrat |
DE102018130440A1 (de) | 2017-11-30 | 2019-06-06 | Mitsubishi Hitec Paper Europe Gmbh | Vorrichtung zur Trocknung eines auf ein Substrat aufgebrachten Fluidfilms sowie Verfahren damit und getrocknetes Substrat |
CN109028872A (zh) * | 2018-07-02 | 2018-12-18 | 陈敏珍 | 一种布料加工用平台输送干燥装置 |
Family Cites Families (20)
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US2272776A (en) * | 1936-07-24 | 1942-02-10 | Armstrong Cork Co | Apparatus for presetting wear films |
NL7609250A (nl) * | 1976-08-20 | 1978-02-22 | Oce Van Der Grinten Nv | Drooginrichting. |
US4365423A (en) | 1981-03-27 | 1982-12-28 | Eastman Kodak Company | Method and apparatus for drying coated sheet material |
DE3900957A1 (de) | 1989-01-14 | 1990-07-19 | Hoechst Ag | Verfahren und vorrichtung zum trocknen einer auf einem durch eine trocknungszone bewegten traegermaterial aufgebrachten fluessigkeitsschicht |
DE3927627A1 (de) | 1989-08-22 | 1991-02-28 | Hoechst Ag | Verfahren und vorrichtung zum trocknen einer auf einem bewegten traegermaterial aufgebrachten fluessigkeitsschicht |
US5290341A (en) * | 1992-08-26 | 1994-03-01 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Fast response membrane generator using heat accumulation |
US5423260A (en) * | 1993-09-22 | 1995-06-13 | Rockwell International Corporation | Device for heating a printed web for a printing press |
DE19503775C1 (de) | 1995-02-04 | 1996-03-14 | Burkamp En Und Anlagentechnik | Verfahren zur Trocknung von Lacken mittels Infrarotstrahlern |
JP2000329463A (ja) * | 1999-05-14 | 2000-11-30 | Konica Corp | 塗膜の乾燥方法及び乾燥装置 |
JP3658355B2 (ja) * | 2001-10-03 | 2005-06-08 | Hoya株式会社 | 塗布膜の乾燥方法、塗布膜の形成方法、及び塗布膜形成装置 |
JP4201259B2 (ja) * | 2002-08-22 | 2008-12-24 | 日東電工株式会社 | 被膜シートの製造方法 |
WO2004078363A1 (ja) * | 2003-03-07 | 2004-09-16 | Nitto Denko Corporation | 塗布膜の乾燥方法および光学フィルム |
JP4616581B2 (ja) * | 2004-06-02 | 2011-01-19 | 富士機械工業株式会社 | 乾燥装置 |
US20060192317A1 (en) * | 2005-02-25 | 2006-08-31 | Paulson Jack E | Method and apparatus for drying coated sheet material |
KR100629655B1 (ko) * | 2005-05-10 | 2006-10-04 | (주) 경일테크 | 양면 전사가 된 원단을 비 가압식으로 건조시키는 장치 |
JP4901395B2 (ja) * | 2006-09-26 | 2012-03-21 | 富士フイルム株式会社 | 塗布膜の乾燥方法 |
JP4805862B2 (ja) * | 2007-02-21 | 2011-11-02 | 富士通セミコンダクター株式会社 | 基板処理装置、基板処理方法、及び半導体装置の製造方法 |
EP2218519A4 (de) * | 2007-11-14 | 2012-03-21 | Fujifilm Corp | Verfahren zum trocknen eines beschichtungsfilms und verfahren zur herstellung eines vorläufers für eine lithographische druckplatte |
JP5422230B2 (ja) * | 2008-03-17 | 2014-02-19 | 富士フイルム株式会社 | 多孔フィルムの製造方法及び装置 |
CN201569264U (zh) * | 2009-08-21 | 2010-09-01 | 上海友浦塑胶有限公司 | 干燥机 |
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2012
- 2012-07-20 BR BR112014002515A patent/BR112014002515A2/pt not_active IP Right Cessation
- 2012-07-20 CN CN201280038430.1A patent/CN103814266B/zh active Active
- 2012-07-20 EP EP12741294.8A patent/EP2739923B1/de active Active
- 2012-07-20 RU RU2014107511A patent/RU2647192C2/ru not_active IP Right Cessation
- 2012-07-20 WO PCT/EP2012/064305 patent/WO2013017441A1/de active Application Filing
- 2012-07-20 JP JP2014523279A patent/JP2014527148A/ja active Pending
- 2012-07-20 KR KR1020147005107A patent/KR20140068039A/ko not_active Application Discontinuation
- 2012-07-20 CA CA2843492A patent/CA2843492A1/en not_active Abandoned
- 2012-07-20 PL PL12741294.8T patent/PL2739923T3/pl unknown
- 2012-07-20 US US14/234,708 patent/US9851144B2/en not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
---|
See references of WO2013017441A1 * |
Also Published As
Publication number | Publication date |
---|---|
JP2014527148A (ja) | 2014-10-09 |
RU2647192C2 (ru) | 2018-03-14 |
CA2843492A1 (en) | 2013-02-07 |
WO2013017441A1 (de) | 2013-02-07 |
US9851144B2 (en) | 2017-12-26 |
EP2739923B1 (de) | 2016-06-29 |
RU2014107511A (ru) | 2015-09-10 |
KR20140068039A (ko) | 2014-06-05 |
PL2739923T3 (pl) | 2016-12-30 |
BR112014002515A2 (pt) | 2017-03-14 |
CN103814266A (zh) | 2014-05-21 |
US20140215844A1 (en) | 2014-08-07 |
CN103814266B (zh) | 2016-01-06 |
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