EP4139618A1 - Procédé de séchage d'un produit exposé à un rayonnement et dispositif d'exposition à un rayonnement infrarouge pour mettre en oeuvre ledit procédé - Google Patents

Procédé de séchage d'un produit exposé à un rayonnement et dispositif d'exposition à un rayonnement infrarouge pour mettre en oeuvre ledit procédé

Info

Publication number
EP4139618A1
EP4139618A1 EP21721440.2A EP21721440A EP4139618A1 EP 4139618 A1 EP4139618 A1 EP 4139618A1 EP 21721440 A EP21721440 A EP 21721440A EP 4139618 A1 EP4139618 A1 EP 4139618A1
Authority
EP
European Patent Office
Prior art keywords
reflector
cooling gas
space
exhaust air
inlet openings
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.)
Pending
Application number
EP21721440.2A
Other languages
German (de)
English (en)
Inventor
Jens Büngener
Doerte EGGERS
Vincent Krafft
Michael Tittmann
Larisa Von Riewel
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Heraeus Noblelight GmbH
Original Assignee
Heraeus Noblelight GmbH
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 Heraeus Noblelight GmbH filed Critical Heraeus Noblelight GmbH
Publication of EP4139618A1 publication Critical patent/EP4139618A1/fr
Pending legal-status Critical Current

Links

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
    • F26B3/28—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
    • F26B3/30—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41F—PRINTING MACHINES OR PRESSES
    • B41F23/00—Devices for treating the surfaces of sheets, webs, or other articles in connection with printing
    • B41F23/04—Devices for treating the surfaces of sheets, webs, or other articles in connection with printing by heat drying, by cooling, by applying powders
    • B41F23/0403—Drying webs
    • B41F23/0406—Drying webs by radiation
    • B41F23/0413—Infrared dryers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41J—TYPEWRITERS; SELECTIVE PRINTING MECHANISMS, i.e. MECHANISMS PRINTING OTHERWISE THAN FROM A FORME; CORRECTION OF TYPOGRAPHICAL ERRORS
    • B41J11/00—Devices or arrangements  of selective printing mechanisms, e.g. ink-jet printers or thermal printers, for supporting or handling copy material in sheet or web form
    • B41J11/0015—Devices or arrangements  of selective printing mechanisms, e.g. ink-jet printers or thermal printers, for supporting or handling copy material in sheet or web form for treating before, during or after printing or for uniform coating or laminating the copy material before or after printing
    • B41J11/002—Curing or drying the ink on the copy materials, e.g. by heating or irradiating
    • B41J11/0021—Curing or drying the ink on the copy materials, e.g. by heating or irradiating using irradiation
    • B41J11/00216—Curing or drying the ink on the copy materials, e.g. by heating or irradiating using irradiation using infrared [IR] radiation or microwaves
    • 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
    • D21F5/001—Drying webs by radiant heating
    • D21F5/002—Drying webs by radiant heating from infrared-emitting elements
    • 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
    • F26B13/101—Supporting materials without tension, e.g. on or between foraminous belts
    • F26B13/104—Supporting materials without tension, e.g. on or between foraminous belts supported by fluid jets only; Fluid blowing arrangements for flotation dryers, e.g. coanda nozzles
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06—Controlling, e.g. regulating, parameters of gas supply
    • F26B21/12—Velocity of flow; Quantity of flow, e.g. by varying fan speed, by modifying cross flow area

Definitions

  • the invention relates to a method for at least partial drying of an irradiation material moved in a transport direction and a transport plane through a process space, the transport plane dividing the process space into an irradiation space and a reflector space, comprising the process steps:
  • the invention relates to an infrared irradiation device for drying an irradiation material moved through a process space in a transport direction and a transport plane, the transport plane dividing the process space into an irradiation space and a reflector space, with a radiator unit with at least one infrared radiator for emitting infrared radiation in the Irradiation room, and with a counter reflector with a reflector wall facing the transport plane, the reflector wall having a plurality of inlet openings for the inlet of cooling gas into the reflector chamber.
  • Such infrared irradiation devices are used, for example, for drying inks, paints, lacquers, adhesives or other solvent-containing layers, in particular for drying sheet-like or web-like printing materials made of paper, cardboard, cardboard, foil or textiles.
  • inks for example, for drying inks, paints, lacquers, adhesives or other solvent-containing layers, in particular for drying sheet-like or web-like printing materials made of paper, cardboard, cardboard, foil or textiles.
  • the emitter unit comprises at least one, usually several infrared emitters. These have, for example, an emission wavelength in the range from about 800 to 2750 nm and generally have to be actively cooled, especially in tight installation spaces, as are typical, for example, in printing machines. Particularly when working radiation in the short-wave infrared range is used, the transmissivity of the printing material can be high, as is the case with paper, for example. Therefore, when using irradiation devices operating in the near infrared (between 800 and 1500 nm), a counter reflector is often provided on the side of the printing material facing away from the emitter unit. One of its main functions is to increase the efficiency of the heating or drying process through multiple reflections.
  • modern IR irradiation devices have an air management system for the regulation of supply air and exhaust air of process gas for drying as well as for cooling.
  • EP 2232 181 B1 describes an IR irradiation device in a chamber design for drying a coating on a quasi-endless carrier which is passed through a transport channel for the material to be irradiated. On one side of the transport channel, several infrared radiation emitting infrared radiation are combined to form a radiator block. A counter reflector block is arranged opposite this and on the other side of the transport channel.
  • the IR irradiation device is surrounded by a housing made of metal profiles, in which fans for cooling the radiators, the material to be irradiated and the counter reflector are accommodated.
  • the counter reflector One function of the counter reflector is to reflect the radiation transmitted through the material to be irradiated in order to intensify the infrared radiation on the material to be irradiated itself by means of multiple reflections. Another function of the counter reflector is to act as a water or air cooled thermal insulator to protect other components of the system from heat.
  • the infrared dryer comprises two infrared emitters, which are assigned to the upper side of the web-shaped material.
  • a counter reflector is assigned to the underside of the material. The counter reflector has a large number of air outlet openings so that both the upper side and the lower side of the material are evenly flushed with cooling air.
  • Typical ingredients of paints, printing inks and inks are oils, resins, water and binders.
  • solvent-based and, above all, water-based printing inks and varnishes drying is necessary, which can be based on physical drying processes through the use of temperature and convection.
  • a common drying strategy is two-stage.
  • rapid pre-drying using infrared radiation is aimed for in order to heat the printing material and bring the printing ink to the so-called "gel point" as quickly as possible.
  • the binders form a three-dimensional network in which color pigments are included. With further removal of solvent and other components, further immobilization occurs and the so-called “critical point” is reached.
  • the network structure there is so rigid that the binders and the pigment can no longer move.
  • the final drying takes place, which only causes the removal of residual moisture, whereby convective drying measures are also used.
  • the invention is therefore based on the object of specifying a drying process which is effective and fast on the one hand, which leads to an improved result in a reproducible manner with regard to the bubble formation mentioned, and which avoids condensation in the reflector space as much as possible.
  • the invention is based on the object of providing an irradiation device for the drying process, which is characterized, in particular for drying solvent-based and especially water-based printing inks, by high speed drying with simultaneous low bubble formation, and which avoids condensation in the reflector space as much as possible.
  • this object is achieved according to the invention, based on a method of the type mentioned at the outset, in that exhaust air is discharged from the reflector space via at least one outlet opening in the reflector wall.
  • the transport level divides the process space into two half spaces, one of which extends between the reflector wall and the material to be irradiated and is referred to here as the “reflector space”.
  • the counter reflector has a gas-permeable reflector wall.
  • the cooling gas flowing out of the inlet openings into the reflector space strikes the material to be irradiated, specifically on the side of the material to be irradiated that faces away from the emitter unit. As a rule, this side is not coated and is also referred to below as the “rear side” of the material to be irradiated.
  • the cooling gas cools the reflector wall and, on the other hand, it interacts with the material to be irradiated by cooling it and, if necessary, also contributing to drying. This can reduce the blustering effect described above.
  • the irradiation power must be adapted to the least absorbing printing ink. Therefore, especially when drying coatings with a color component in the black or cyan range, which absorbs infrared radiation particularly well, high temperature peaks can occur.
  • the cooling of the material to be irradiated by the cooling gas flowing towards the back of the material to be irradiated counteracts excessive and excessive heating of the material to be irradiated, resulting in a comparatively mild drying of the material to be irradiated contributes in this drying phase.
  • the radiation power and thus the transport speed can be increased without damaging the material to be irradiated or the coating on it.
  • the gas-permeable counter-reflector thus not only fulfills the usual functionalities described above, but also, as a result of the introduction of the cooling gas through the inlet openings of the reflector wall, it also interacts with the material being irradiated in the transport plane, which enables a controlled temperature development in the material to be irradiated, which is undesirable Can reduce phenomena such as blistering.
  • Exhaust air is discharged from the reflector space via at least one outlet opening in the gas-permeable reflector wall, preferably via several outlet openings.
  • the moisture contained in lacquers or paints evaporates when heated and can condense in cooler places, such as on the actively cooled wall of the counter-reflector, and form incrustations there and impair the functionality of the system, for example the reflectivity of the counter-reflector. If the reflector wall has inlet openings for the cooling gas and an outlet opening or several outlet openings through which the exhaust air flows out is discharged from the reflector space, moisture can also be removed with the exhaust air from the rear area of the material to be irradiated, thus avoiding condensation.
  • the amount of cooling gas can be varied continuously or in stages. It is achieved, for example, by a location-dependent control of the amount of cooling gas introduced through the inlet openings and / or by the fact that the total opening cross-section of the inlet openings increases or decreases in the transport direction in uniformly large partial areas of the gas-permeable reflector wall.
  • the temperature of the material to be irradiated is measured at several positions distributed along the process chamber in the direction of transport.
  • a temperature profile is obtained over the material to be irradiated as it moves through the process space.
  • the temperature profile can be used to regulate the amount of cooling gas
  • exhaust air is discharged from the reflector space via several outlet openings in the gas-permeable reflector wall.
  • the cooling gas flows into the reflector chamber through the inlet openings from a gas distribution chamber adjoining the gas-permeable reflector wall.
  • the gas-permeable reflector wall closes off the gas distribution chamber on one side.
  • the cooling gas is introduced into the gas distribution chamber at one point or at several points and flows out of the gas distribution chamber through the inlet openings of the reflector wall into the reflector space.
  • a uniform cooling gas pressure can be established within the gas distribution chamber, so that the amount of gas flowing out is determined solely by the distribution and the opening cross-section of the inlet openings. Preferred procedures of the method are explained below, in which the gas-permeable reflector wall is part of a gas distribution chamber.
  • the gas distribution chamber is subdivided into several sub-chambers, the amount of cooling gas flowing into the reflector chamber through inlet openings varying from sub-chamber to sub-chamber as viewed in the transport direction.
  • pressures of the cooling gas that are independent of one another can be set.
  • the amount of cooling gas flowing out of the respective sub-chamber into the reflector space then depends on the respective gas pressure and on the respective total opening cross-section of the inlet openings. With an increase in the amount of cooling gas, a temperature of the material to be irradiated that increases in the direction of transport can be at least partially compensated for.
  • a variant of the method is preferred in which at least a first of the sub-chambers is provided with a first cooling gas connection, via which a first cooling gas flow is supplied to first inlet openings, and in which a second of the sub-chambers is provided with a second cooling gas connection , via which a second cooling gas flow is fed to second inlet openings, the first cooling gas flow being adjustable independently of the second cooling gas flow.
  • the gas distribution chamber is advantageously provided with an exhaust air connection via which at least part of the exhaust air is diverted from the reflector space.
  • an exhaust air connection via which at least part of the exhaust air is diverted from the reflector space.
  • the gas-permeable reflector wall in addition to the inlet openings, also has outlet openings which open into the sub-chamber with the exhaust air connection. Used exhaust air is removed from the reflector space through the outlet openings and sucked into the sub-chamber equipped with the exhaust air connection and discharged from there. Separate controllability of the exhaust air and the cooling gas supply air ensures that moisture-laden exhaust air is largely extracted from the reflector space and condensation can be avoided.
  • the cooling of the counter reflector and the interaction of the cooling gas with the material to be irradiated are preferably carried out independently of a process gas quantity control, by means of which process gas is introduced into the process room via an air supply unit and used exhaust air is discharged from the process room via an exhaust air unit.
  • the process gas is primarily used to remove moisture from the material to be irradiated, whereas the cooling gas is primarily used to control the temperature of the counter reflector and the material to be irradiated. Both functions can be fulfilled by one and the same gas; in the simplest case, the process gas and the cooling gas are air.
  • the above-mentioned object is achieved according to the invention, based on a device of the type mentioned at the beginning, in that the reflector wall has at least one outlet opening for the discharge of exhaust air from the reflector space.
  • the transport level divides the process space into two half spaces, one of which extends between the reflector wall and the material to be irradiated and is referred to here as the “reflector space”.
  • the inlet openings are designed so that cooling gas flows through them into the reflector space and in the process strikes the material to be irradiated, specifically on the rear side of the material to be irradiated, facing away from the emitter unit.
  • the cooling gas cools the reflector wall and, on the other hand, it interacts with the material to be irradiated by cooling it and, if necessary, also contributing to drying.
  • the blustering effect can be reduced, as explained in more detail above with reference to the method according to the invention.
  • the gas-permeable counter-reflector not only fulfills the usual functionalities described above, but also, as a result of the introduction of the cooling gas through the inlet openings in the reflector wall, interacts with the material being irradiated in the transport plane, which enables a controlled temperature development in the material to be irradiated, which causes undesirable phenomena to occur such as blistering.
  • the gas-permeable reflector wall has at least one outlet opening, preferably several outlet openings for the discharge of exhaust air from the reflector space.
  • the reflector wall also has an outlet opening or several outlet openings for discharging exhaust air from the reflector space, moisture is also removed with the exhaust air, thus avoiding condensation.
  • the number and / or the opening cross-section of the inlet openings varies.
  • a variation in the opening cross-section is measured by whether the total opening cross-section of the inlet openings - determined in uniformly large partial areas of the reflector wall - increases or decreases viewed in the direction of transport.
  • the reflector wall is subdivided into several sections, viewed in the direction of transport, and that the number and / or the total opening cross-section of the inlet openings varies from section to section.
  • the sections of the reflector wall differ in terms of their permeability for the cooling gas in the sense that the gas permeability increases or decreases from section to section.
  • the gas permeability which increases in the direction of transport, enables an increasing amount of cooling gas to flow into the reflector space and to at least partially compensate for a temperature of the material to be irradiated that increases in the direction of transport. Even if the gas-permeable reflector wall is subdivided into several differently designed sections, a one-piece design of the reflector wall is preferred.
  • the temperature sensors are distributed along the reflector wall as seen in the direction of transport.
  • the temperature of the material to be irradiated can be detected as it moves through the process space at several positions, for example at 2 to 8 positions, preferably at 2 to 5 positions.
  • the temperature profile determined in the process can be used to regulate the amount of cooling gas.
  • the temperature sensors are preferably designed for contactless temperature measurement, for example as pyrometers.
  • the gas-permeable reflector wall has a plurality of outlet openings for discharging exhaust air from the reflector space.
  • the number and / or the total opening cross-section of the outlet openings can vary in the transport direction, so that the amount of exhaust air discharged from the reflector space can also be varied; in particular, it can increase in the direction of transport.
  • One embodiment of the irradiation device is characterized in that the reflector wall adjoins a gas distribution chamber.
  • the gas-permeable reflector wall closes off the gas distribution chamber on one side.
  • the cooling gas can be introduced into the gas distribution chamber at one point or at several points, and from there it flows through the inlet openings of the reflector wall into the reflector space.
  • a uniform cooling gas pressure can be established within the gas distribution chamber, so that the amount of cooling gas flowing out is determined solely by the distribution and the opening cross section of the outlet openings.
  • the gas distribution chamber is divided into several sub-chambers.
  • Cooling gas pressures which differ from subchamber to subchamber, can be set in subchambers within the gas distribution chamber that are fluidically separated from one another.
  • the amount of cooling gas flowing out from subchamber to subchamber can thus be changed and is determined by the cooling gas pressure and the distribution and the total opening cross section of the outlet openings of the respective subchamber.
  • the amount of cooling gas flowing into the reflector space through the inlet openings of the reflector wall can vary, for example, from subchamber to subchamber (viewed in the direction of transport).
  • the gas distribution chamber is advantageously provided with an exhaust air connection via which at least part of the exhaust air is diverted from the reflector space. In the case of a subdivision of the gas distribution chamber into several sub-chambers, it has also proven to be advantageous if at least one of the sub-chambers is provided with such an exhaust air connection.
  • the gas-permeable reflector wall has, in addition to the inlet openings, an outlet opening or several outlet openings which open into the sub-chamber with the exhaust air connection.
  • the exhaust air can be removed from the reflector space through the outlet openings and introduced into the partial chamber equipped with the exhaust air connection and discharged from there to the outside. Separate controllability of the exhaust air and cooling gas supply air ensures that moisture-laden exhaust air is largely extracted from the reflector space and condensation can be avoided.
  • At least a first of the sub-chambers is provided with a first cooling gas connection via which a first cooling gas flow is supplied to first inlet openings, and a second of the sub-chambers is provided with a second cooling gas connection, via which a second cooling gas flow is supplied to second inlet openings, the first cooling gas flow being adjustable independently of the second cooling gas flow.
  • the irradiation device advantageously has, independently of the gas-permeable counter-reflector, a process gas supply unit for introducing process gas into the process space and an exhaust air unit for discharging exhaust air from the process space.
  • the cooling of the counter reflector and the interaction of the cooling gas with the material to be irradiated can take place independently of a process gas quantity control, by means of which process gas is introduced into the process room via an air supply unit and exhaust air is discharged from the process room via an exhaust air unit.
  • the reflector wall is provided with inlet openings and optionally with outlet openings. It consists of one piece or it is composed of several reflector wall pieces. If necessary, the reflector wall pieces can differ in the area occupied by the inlet openings, and possibly also in the area occupied by their outlet openings.
  • the reflector wall preferably forms a wall of a gas distribution chamber.
  • the gas distribution chamber consists of a single chamber or it is made up of several parts and is formed by several sub-chambers. If necessary, the sub-chambers are closed off by a common reflector wall, or each of the sub-chambers has its own reflector wall.
  • the sub-chambers are fluidically connected to one another, or they are fluidically separated from one another and optionally designed for processing different gas quantities and / or gas pressures.
  • Figure 1 shows a printing machine with a printing unit and an infrared
  • FIG. 2 shows a sketch of an irradiation device as part of the dryer system of the printing machine from FIG. 1 in a longitudinal section
  • FIG. 3 shows a three-dimensional representation of an embodiment of the
  • FIG. 4 shows a gas distribution chamber of the irradiation device with the flow profile of the cooling air drawn in
  • FIG. 5 the gas distribution chamber of the irradiation device with the flow profile of the exhaust air drawn in
  • FIG. 6 shows a three-dimensional representation of an embodiment of the irradiation device in the assembly
  • FIG. 7 shows a diagram with temperature profiles on the surface of the material to be irradiated along the process chamber during processing with and without a gas-permeable counter-reflector.
  • FIG. 1 schematically shows a printing machine in the form of a web-fed inkjet printing machine to which the reference number 1 is assigned as a whole.
  • the material web 3 from a printing material arrives at a printing unit 40.
  • This comprises several inkjet print heads 4 arranged one behind the other along the material web 3, through which solvent-based and in particular water-based printing inks are applied to the printing material.
  • the material web 3 passes from the printing assembly 40 via a deflection roller 6 to an infrared dryer system 70.
  • This is equipped with several dryer modules 7, which are designed for drying the solvent in the material web 3.
  • the drying modules 7 are each equipped with a counter-reflector unit 23 with a gas-permeable counter-reflector and are explained in more detail below with reference to FIGS. 2 to 7.
  • the further transport path of the material web 3 goes via a tension roller 8, which is equipped with its own tension drive motor and via which the web tension is set, to a take-up roller 9.
  • Each of the dryer modules 7 is equipped with several infrared radiators - in the exemplary embodiment there are eighteen.
  • a heating filament made of carbon or tungsten in a spiral or ribbon form is enclosed in an inert gas-filled radiator tube, which is usually made of quartz glass is made.
  • the heating filaments are connected to electrical connections that are inserted through one or both ends of the radiator tube.
  • the dryer modules are arranged in pairs next to and behind one another in the dryer system as seen in the direction of transport.
  • the pair of dryer modules 7 arranged next to one another covers the maximum format width of the printing machine 1.
  • the dryer modules 7 and the individual infrared radiators can be electrically controlled separately from one another in accordance with the dimensions and color coverage of the printing material.
  • the dryer module is equipped with sheet-like infrared heater panels instead of the tubular infrared heater.
  • the infrared radiator panels comprise a substrate made of an infrared radiation-emitting material and are covered with a conductor track or with several conductor tracks made of resistance material for the thermal excitation of the infrared emission. In the case of an occupancy with several conductor tracks, these can be controlled separately from one another in order to generate a non-homogeneous temperature profile over the infrared radiator surface.
  • the transport speed of the material web 3 is set to 5 m / s. This is a comparatively high speed that requires a high drying rate.
  • the drying process required to achieve this requirement and the irradiation device used for this are explained in more detail below with reference to FIGS. 2 to 7. If the same reference numerals are used in these figures as in FIG. 1, these designate identical or equivalent components and components, as explained in more detail above with reference to the description of the printing press.
  • the sketch of Figure 2 shows an irradiation device arranged on the material web 3 in the form of a drying module 7.
  • the drying module 7 is composed of a radiator unit 22 and a counter-reflector unit 23, separated from one another by the material web 3 moving in the transport level 3a.
  • the radiator unit 22 is equipped with several elongated infrared radiators 24, the longitudinal axes of which run perpendicular to the transport direction 5 and which are arranged parallel to one another.
  • the radiator unit 22 has its own Air management system equipped, which comprises a supply air unit 25 for the supply of drying air and an exhaust air unit 26 for the discharge of used air.
  • the supply and exhaust air unit (25; 26) is independent of the counter reflector unit 23 described in more detail below and is used in particular to dissipate excess heat in the rear space of the radiator unit 22 in order to protect the surrounding parts of the printing press 1 from overheating.
  • the counter reflector unit 23 comprises a gas distribution chamber 27 which is equipped with an air inlet 28, an air outlet 29 and reflector plate 30 provided with a plurality of through-bores.
  • the gas-permeable reflector plate 30 is a wall of the gas distribution chamber 27 facing the material web 3. It delimits the gas distribution chamber 27 at the top and the reflector space 33 at the bottom.
  • a plurality of pyrometers 34 are arranged within the gas distribution chamber 27, which pyrometers are distributed in the transport direction 5 along the reflector plate 30 and are designed to measure the temperature of the underside of the material web.
  • the transport plane 3 a divides the process space 31 into an irradiation space 32 facing the emitter unit 22 and a reflector space 33 facing the counter reflector unit 23.
  • FIG. 3 shows a three-part counter-reflector unit 23. This is constructed in a modular manner from three reflector chambers that are fluidically connected to one another and is encompassed by a common, one-part frame 35. From the top view of the material web 3 (which simultaneously defines the transport plane 3a) and the counter-reflector unit 23, the reflector plate 30 can be seen, which in this embodiment consists of three reflector plate fields 30a, 30b, 30c, each with a different distribution of inlet and outlet openings (36; 37) composed.
  • the reflector plate 30 has a large number of through-bores, which are divided into small, closely-meshed, circular inlet openings 36 and oval outlet openings 37. Seen from bottom to top (that is, in the transport direction 5), thirteen rows of circular inlet openings 36 offset from one another are provided, which are followed by two rows of oval outlet openings 37. To come after eleven rows of inlet openings 36, again two rows of outlet openings 37, another ten rows of inlet openings 36, another two rows of outlet openings 37, another ten rows of inlet openings 36, and finally three rows of oval outlet openings 37.
  • the circular inlet openings 36 have an inner diameter of 4 mm and the oval ones Outlet openings 37 have an opening cross-section of 353mm 2 .
  • the number of outlet openings 37 and / or the total opening cross-section of outlet openings 37 thus increase in the transport direction 5, so that in this direction more and more moisture-laden or used cooling gas than exhaust air from the reflector space 33 into the air outlet 29 of the counter-reflector unit 23 is discharged.
  • the inlet openings 36 are fluidically connected to two gas inlet ports 38a; 38b (better to be seen in FIG. 4) is connected to the gas distribution chamber 27 for the supply of dry air into the reflector space 33.
  • the outlet openings 37 are fluidically connected to a gas outlet connector 39 (better to be seen in FIG. 5) of the gas distribution chamber 27 for the discharge of used air from the reflector space 33.
  • the opening dimensions and the number and distribution of the through bores 36; 37 are adapted to the type of product to be irradiated and the emitter power.
  • the temperature of the material to be irradiated increases in the transport direction, so that a number of inlet openings 36 are required for adequate and uniform cooling; on the other hand, the air humidity also increases steadily, so that a certain number of outlet openings 37 is also necessary.
  • the area occupied by the outlet openings 37 increases in the direction of transport, and as a result the area occupied by the inlet openings 36 inevitably decreases.
  • the specific design can be optimized based on the above information and the exemplary embodiment for the application, the heater type and the heater power, for example empirically through practical tests and / or theoretically using simulations.
  • the reflector plate 30 is suitable for reflecting infrared radiation and the reflector plate material should itself be heat-resistant and preferably also be heat-conductive.
  • the reflective plate 30 is made of anodized aluminum.
  • the reflector plate 30 is made of aluminum metallic surface, stainless steel, in particular polished stainless steel or other metals, in particular made of precious metals or from a workpiece that is coated with one of the materials mentioned. As seen in the transport direction 5, the area occupied by the outlet openings 37 increases and that of the inlet openings 36 decreases.
  • the three-dimensional views of the counter reflector unit 23 from FIG. 4 and FIG. 5 show that the gas distribution chamber 27 is divided into several sub-chambers by means of partition walls 41, two of which are sub-chambers each with one of the gas inlet nozzles 38a; 38b, and the third sub-chamber is connected to the gas outlet nozzle 39.
  • the flow lines 42 in FIG. 4 indicate the distribution of the dry cooling air from the two gas inlet nozzles 38a; 38b to the inlet openings 36.
  • the flow lines 43 indicate the distribution of the used exhaust air from the outlet openings 37 to the gas outlet connection 39.
  • the supply of the dry cooling air via the gas inlet nozzle 38a; 38b and the discharge of the used exhaust air via the gas outlet nozzle 39 can be regulated separately from one another.
  • FIG. 6 shows a dryer module 7 assembled from two radiator units 22a, 22b and a two-part counter-reflector unit 23.
  • the counter-reflector unit 23 with a gas-permeable reflector plate 30 is used.
  • the cooling air flowing from the inlet openings 36 of the reflector plate 30 against the uncoated underside of the material web 3 causes a uniform temperature development in the printing material (paper). This is helped by the fact that several reflector plate fields 30a, 30b, 30c with an adapted distribution of inlet openings 36 and outlet openings 37 are used.
  • the amount of exhaust air extracted is comparatively small when the material web 3 enters the process chamber 31 and increases until it exits the process chamber 31.
  • the rear cooling of the material web 3 by the incoming cooling air counteracts excessive and rapid heating of the material to be irradiated between the reaching of the gel point and the critical point, which contributes to a comparatively mild drying of the material to be irradiated in the first drying phase.
  • a comparatively more homogeneous temperature profile is established.
  • the radiation output and thus the transport speed can be increased without damaging the irradiated item or the respondent on it.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Textile Engineering (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

Les dispositifs d'exposition à un rayonnement infrarouge connus servant à sécher un produit exposé à un rayonnement (3) déplacé dans une chambre de traitement (31) présentent une unité d'émission de rayonnement (22) dotée d'au moins un émetteur de rayons infrarouges (24) destiné à émettre un rayonnement infrarouge ainsi qu'un contre-réflecteur (23) muni d'une paroi de réflexion (30), ladite paroi de réflexion (30) comportant une pluralité d'ouvertures d'entrée (36) destinées à permettre l'entrée de gaz de refroidissement dans la chambre de réflecteur (33). L'invention vise à mettre au point sur cette base un dispositif d'exposition à un rayonnement pour le procédé de séchage, dispositif se caractérisant en particulier, pour le séchage d'encres d'impression contenant des solvants et en particulier à base d'eau, par une grande rapidité de séchage avec simultanément une formation réduite de bulles et une faible condensation dans la chambre de réflecteur. A cet effet, selon l'invention pour évacuer l'air sortant hors de la chambre de réflecteur (33), la paroi de réflecteur (30) présente au moins une ouverture de sortie (37).
EP21721440.2A 2020-04-22 2021-04-21 Procédé de séchage d'un produit exposé à un rayonnement et dispositif d'exposition à un rayonnement infrarouge pour mettre en oeuvre ledit procédé Pending EP4139618A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102020110912.1A DE102020110912A1 (de) 2020-04-22 2020-04-22 Verfahren zum Trocknen eines Bestrahlungsguts und Infrarot-Bestrahlungsvorrichtung zur Durchführung des Verfahrens
PCT/EP2021/060355 WO2021214128A1 (fr) 2020-04-22 2021-04-21 Procédé de séchage d'un produit exposé à un rayonnement et dispositif d'exposition à un rayonnement infrarouge pour mettre en œuvre ledit procédé

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Publication Number Publication Date
EP4139618A1 true EP4139618A1 (fr) 2023-03-01

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US (1) US20230221071A1 (fr)
EP (1) EP4139618A1 (fr)
JP (1) JP7454701B2 (fr)
CN (1) CN115427749B (fr)
DE (1) DE102020110912A1 (fr)
WO (1) WO2021214128A1 (fr)

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CN216631458U (zh) * 2021-11-05 2022-05-31 江苏时代新能源科技有限公司 风嘴及涂布机

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JPS4992649A (fr) * 1972-12-27 1974-09-04
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FI80099C (fi) 1986-10-31 1990-04-10 Imatran Voima Oy Foerfarande och anordning foer torkning av roerligt banmaterial.
JP2002267356A (ja) * 2001-03-12 2002-09-18 Daito Seiki Co Ltd 遠赤外線乾燥装置、乾燥装置構成体及び乾燥方法
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JP2006226629A (ja) * 2005-02-18 2006-08-31 Negishi Seisakusho:Kk 輻射乾燥装置
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WO2010089936A1 (fr) * 2009-02-04 2010-08-12 シャープ株式会社 Appareil de séchage d'encre
JP5421934B2 (ja) * 2011-01-13 2014-02-19 東京エレクトロン株式会社 電極製造装置、電極製造方法
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CN115427749A (zh) 2022-12-02
US20230221071A1 (en) 2023-07-13
WO2021214128A1 (fr) 2021-10-28
DE102020110912A1 (de) 2021-10-28
JP7454701B2 (ja) 2024-03-22
CN115427749B (zh) 2024-06-28
JP2023523728A (ja) 2023-06-07

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