This application is the U.S. National Phase, under 35 U.S.C. ยง 371, of PCT/EP2019/059858, filed Apr. 16, 2019; published as WO 2019/201960 A1 on Oct. 24, 2019, and claiming priority to DE 10 2018 206 154.8, filed Apr. 20, 2018, the disclosures of which are incorporated herein in their entireties by reference.
The present invention relates to a processing machine having a drying device, in particular a machine for processing printing material or sheets or for processing substrate, specifically a printing press, and to a method for operating a drying device in a processing machine.
High-performance drying devices comprising radiation dryers, in particular, are typically cooled. UV emitters installed in a UV module, for example, in printing material processing machines, for example sheet-fed printing presses, are cooled especially during operation. UV emitters operating at higher outputs must also be cooled to prevent them from reaching the transformation temperature of the glass tube, causing the tube to become deflected or even to blow out.
Exhaust air cooling systems for cooling UV emitters are known. In such systems, ambient air flows through an air inlet opening in the housing past the UV emitter, with the air inlet opening also acting at the same time as the radiation outlet opening. The disadvantage of such systems is that, due to its structural configuration, the UV emitter is cooled primarily on its upper side. The underside is generally much hotter because there is insufficient convection there. Heat on the underside is dissipated by the radiation and conduction of heat in the glass tube toward the well-cooled upper side.
From DE 694 13 439 T2 and EP 1 625 016 B1, it is known to use supply air from the air duct of the housing profile to blow air at a UV emitter. This supply air cooling is significantly more effective than exhaust air cooling and substantially reduces the glass tube temperature on the upper side of the UV emitter.
However, its influence on the temperature on the underside of the glass tube is insufficient, since the conduction of heat in the glass tube from the underside to the upper side is limited.
From DE 101 25 770 A1, an irradiation device is known, in which the radiation source is arranged, rotatable about its longitudinal axis, in conjunction with a supply air cooling system in the irradiation device. The disadvantage of this solution is that it functions using a supply air cooling system and comprises moving parts that are susceptible to malfunction, and is therefore complex and inefficient.
From JP 4-132940 U, KR 10-1031749 B1, EP 2 697 066 B1, JP 2014-42884 A and EP 3 168 861 A1 it is known to use a plate to encapsulate drying devices against ambient air, with various airflow routes being implemented in the housing. The disadvantage of these solutions is that a large flow volume of ambient air flowing around the radiation source is not achieved. In addition, an effective extraction of ambient air contaminated with ozone is not provided.
From DE 10 2008 058 056 A1 a UV irradiation device is known, in which a first cooling air flow is drawn into the sides of the housing via air inlet openings in the outer wall in order to cool the bulkhead system from the outside. The cooling air is conducted along the housing wall into a central exhaust duct and from there travels to a blower via a manifold, which forces the entire cooling air flow to the UV irradiation device. A second cooling air flow is captured in the region of the radiation source by a long-necked suction duct and is conducted via a restrictor into the manifold. The disadvantage of this solution is that this exhaust air cooling system does not adequately cool the underside of the radiation source.
From FR 2 774 156 A1, a device is known for accelerating drying by means of an infrared emitter that generates heat. In said device, an air generation system supplies low temperature air to reduce the temperature within the housing.
DE 102 47 464 A1 discloses a dryer device having an infrared emitter, with an after-dryer module situated downstream of a main dryer module. The dryer device is sealed off from the cold ambient air by a bulkhead.
From JP 2000-157925 A, an ultraviolet curing device with a UV radiation tube is known. For cooling, the distance between the reflectors and the emitter over the length of the emitter is adjusted. Additionally, an air duct is used, which directs cooling air directly onto the emitter. The cooling air expelled from the air duct is configured such that it increases in volume as it moves further away from an exhaust side.
The object of the present invention is to create an alternative processing machine having a drying device or an alternative method for operating a drying device in a processing machine. In particular, the object is to improve the cooling of preferably high-performance dryers in processing machines, such as machines for processing substrate or printing material. Particularly preferably, the object is to further improve the cooling of a UV emitter, including on the underside thereof.
The object is achieved according to the invention by the provision of a processing machine having a drying device which comprises a radiation source accommodated in a housing. Shutters are provided adjacent to the radiation source in the housing. The housing has at least one air inlet opening for ambient air so that, once the ambient air has entered the housing, it flows around the radiation source. The housing also has an air outlet opening for exhaust air. A blower air system is associated with the drying device and by which blower air system, ambient air flowing into the air inlet opening is or can be actively influenced at a distance from the radiation source. A method is also provided for operating the drying device in the processing machine. The blower air system, which is associated with the drying device, actively influences or deflects the ambient air flowing into the air inlet opening before it reaches the radiation source.
The invention offers the advantage that an alternative processing machine having a drying device or an alternative method for operating a drying device in a processing machine is created. In particular, the cooling of preferably high-performance dryers in processing machines, such as machines for processing substrate or printing material, in particular printing presses or sheet-processing machines, is improved. Particularly preferably, the cooling of the underside of a UV emitter is further improved.
The drying device is preferably used in a sheet-processing or substrate-processing machine, especially a printing press, or such a machine is equipped with one or more such drying devices. Preferably, the drying device can also optionally be used as an interdeck dryer or as an end-of-press dryer, for example in a delivery. Tabular substrate, for example metal sheets, can be processed as the substrate. However, material in rolled format or sheet format can also be processed, in particular printed or coated.
Exhaust air cooling has the particular advantage that ozone generated by UV radiation is extracted at the same time from the drying device, for example a UV module. Ozone presents a health hazard to humans; moreover, ozone absorbs UV radiation and thus diminishes the curing effect of the drying device, in particular the UV module. A blower air system improves the airflow guidance in the preferred exhaust air cooling system.
The ambient air, in particular the ambient air located outside of the drying device or in contact with a printing material, is preferably guided in a targeted manner by additional directed air and/or blower air in such a way that both the ambient air and the additional air or blower air are optimally guided as cooling air around the radiation source, after which the common cooling air is removed, in particular extracted, as exhaust air through one or more air outlet openings.
In addition, the underside of the radiation source can be cooled directly and/or indirectly by air streams, for example blower air streams or blower air jets, which are introduced on one side or preferably on both sides, with the additional air, for example blower air, being introduced or blown in, in particular, beyond the irradiation range of a UV module. With the preferable introduction or blowing in of air on both sides, the two streams can meet, for example, at the center below the UV module or beneath the radiation source. Alternatively or additionally, part of the air can be blown at the radiation source, in particular a UV emitter, directly from below. Preferably, however, blower air is guided parallel to or within the plane of the air inlet opening of the housing, so that the blower device does not lie within the beam path of the radiation from the radiation source. Thus, the blower air is preferably generated at least approximately parallel to the web of processing material or to a printing material web.
In particular, constricting the ambient air improves or optimizes the transport thereof as cooling air in the drying device, in particular in the UV module, to the underside of the radiation source, thereby better cooling the underside thereof. In addition, cooling advantageously becomes more turbulent and, surprisingly, the upper side of the radiation source is also better cooled, as has been evidenced in studies, specifically on the basis of temperature measurements.
The additional air or blower air is introduced or blown in, for example, over the entire length of a drying device, for example the UV module, or the radiation source. This can be accomplished using air guide elements, such as baffles, and/or blower air openings, in particular nozzles. The air introduced or blown in on both sides, for example, can be either part of or at least approximately all of the cooling air discharged in the UV module. The air flow volume of the air additionally introduced or blown in by the blower air system can preferably be between 20% and 50% of the total cooling air flow volume. Accordingly, the proportion of inflowing ambient air can be between 80% and 50%. The goal, in particular, is a ratio of approximately 1/3 air additionally introduced or blown in by the blower air system and approximately 2/3 incoming ambient air.
The radiation sources, in particular UV emitters, can thus particularly advantageously be operated at an even higher output or the air flow volume can be reduced while the same level of cooling is maintained. As a further advantage, a deflection or blow-out of a UV emitter can be more reliably prevented.
It can further be provided to configure the blower air system as an add-on module or auxiliary module, which can be embodied as detachably or permanently connectable in particular to a UV module of a dryer. Such a blower air system can be configured to be added on to any UV module of a dryer. Said add-on module in particular comprises separate air guiding elements or air ducts, which are provided for influencing or adjusting the ambient air flow volume flowing around the radiation source. An add-on module or auxiliary module can easily be used for retrofitting dryers. Further, a plate spaced a distance from the housing of the UV module could also be additionally provided in the beam path of the radiation source, as long as a sufficient air flow volume flowing into at least one air inlet opening is ensured.
In the following, the invention will be explained in detail by way of example. The accompanying drawings schematically depict the following:
In processing machines such as printing material processing machines, in particular printing presses or sheet processing machines, for example sheet-fed printing presses, in particular sheet-fed rotary offset printing presses, preferably in unit-based and inline configuration, substrates or printing materials are conveyed through the machine. In sheet processing machines, sheets of printing material, for example, are gripped at the leading edge by cylinders or by drums and are conveyed or transported through the machine as the cylinders rotate. The sheets of printing material are transferred between the cylinders in the gripper closure. In printing presses, the printing materials pass through various printing units along the conveying path, in each of which the materials are printed with a respective printing ink in accordance with the desired motif. Each of the printing units may comprise, for example, a plate cylinder, which is inked up by means of an inking unit with the printing ink to be used. This inked-up plate cylinder transfers the printing ink, in accordance with the motif, onto a blanket cylinder furnished with a rubber printing blanket, which cylinder forms a printing nip with a printing cylinder of a sheet-fed printing press, which printing cylinder conveys the sheet of printing material. As it passes through the printing nip, the corresponding motif is transferred from the inked-up rubber printing blanket of the blanket cylinder onto the sheet of printing material.
Downstream of the last printing unit of the printing press, the printed sheets of printing material can be delivered in a delivery of a sheet-fed printing press to form a delivery pile. The last printing unit can also be followed, for example, by one or more coating units, which furnish the printed sheets of printing material with a protective coating or gloss coating. UV inks are preferably used in the printing units and UV coatings are preferably used in the coating units. For recto-verso printing, a printing press may include a turning device. Alternatively, however, other printing methods, for example with variable motifs, can also be used. A drying device or an interdeck dryer in the machine is embodied, in particular, as a UV drying device and comprises one or more UV modules 1, for example.
On the path to the delivery pile, the sheets 4 are guided past the UV modules 1 that dry or cure the sheets 4. The UV modules 1 each have UV emitters 2, the UV radiation of which is directed directly or via reflectors 3 onto the surface of the sheets 4. This UV radiation acting on the sheets 4 dries or cures the treated sheet surface, in particular the printed UV ink and/or the applied UV coating. Preferably, mercury vapor lamps are used as radiation sources in the UV modules 1. Additionally or alternatively, emitters with other wavelengths, such as infrared dryers, for example, can also be used. For example, plug-in slots can be provided in the machine or the delivery, into which the UV modules 1 can be inserted. The UV modules 1 can be fixed in these plug-in slots, thereby ensuring that the UV modules 1 can be replaced, e.g. if the UV emitter 2 becomes worn. The UV modules 1 operate in particular with exhaust air cooling.
The ambient air, which is drawn in between the shutters 9 or reflectors 3 and the UV emitter 2, flows through the air inlet opening 10 that faces the substrate or printing material and thereby cools the UV emitter 2. The cooling air then flows out between the shutters 9 into the exhaust air duct 12 of the housing profile 8. For this purpose, the exhaust air duct 12 is preferably connected on one side to a suction air source that can be controlled or regulated, for example, which draws the exhaust air into the exhaust air duct 12. The exhaust air duct 12 preferably extends over the entire length of the UV emitter 2, so that the air heated at the UV emitter 2 can be drawn off into the exhaust air duct 12 through distributed openings. It can be provided, for example, that the exhaust air duct 12, which extends along the radiation source, in particular the UV emitter 2, can be connected to the space surrounding the UV emitter 2 via oblong holes that are spaced apart from one another. Said oblong holes are preferably dimensioned such that they differ from one another in terms of their aperture areas. In particular, the aperture areas of the oblong holes between the ends of an elongated UV emitter 2 are smaller in dimension than the oblong holes provided at the respective ends of the UV emitter 2. Very preferably, the aperture areas of the oblong holes between the ends of the elongated UV emitter 2 are dimensioned as steadily decreasing in size, in particular without local maxima, toward the suction air source of the exhaust air duct 12. More preferably, the aperture areas of the oblong holes associated with the ends of the elongated UV emitter 2 are dimensioned differently from one another, with the aperture area of at least one oblong hole at the end of the UV emitter 2 that faces the suction air source of the exhaust air duct 12 preferably having smaller dimensions than the aperture area of at least one oblong hole at the end of the UV emitter 2 that faces away from the suction air source of the exhaust air duct 12. The oblong holes that face the respective ends of the UV emitter 2 can also comprise two, three, or four oblong holes.
The air flows that result during operation with exhaust air cooling activated and with the blower air system 13 deactivated are depicted here generally or schematically. Cooling occurs above all on the upper side of the UV emitter 2, while the underside directed toward the processing material is cooled less than the upper side. Warming up can take place in this operating mode, for example. This can also be the operating mode, for example, during operation when the UV module 1 is operating at low output, for example, in particular when the glass tube temperature is low, for example when the emitter output is less than 140 to 120 W/cm.
The blower air jets 17 generated by the blower air system 13 are aligned toward one another in one plane, in particular such that they influence, in particular restrict or constrict, the ambient air flow 11 flowing into the housing profile 8. The blower air jets 17 are preferably directed toward one another in one plane in such a way that they would preferably meet at the center of the air inlet opening 10, for example exactly below the UV emitter 2. The ambient air flow 11 is preferably influenced in such a way that the ambient air flow 11 cools the underside of the UV emitter 2, which faces the processing material or printing material, with increased intensity. In particular, the blower air system 13 generates a cross flow to the ambient air flow 11.
The cooling system or blower air system 13 of the radiation source, in particular of the UV emitter 2, has a maximum cooling capacity here exclusively in a cooling region B between the planes E1, E2 formed by the electrodes 19. A constant cooling output is preferably generated over the entire cooling region B, the cooling region B particularly preferably extending only between the mutually facing surfaces of the electrodes 19. However, the maximum cooling output in the cooling region B can be controlled or adjusted in terms of intensity or effect according to desired requirements. Adjacent to the cooling region B, in particular outside of the planes E1, E2, the cooling output of the cooling system or the blower air system 13 is reduced as compared with the maximum cooling capacity, or preferably is zero. The diameter of the glass body 20 in the present case is larger between the planes E1, E2 or in the cooling region B than in the edge regions. Outside of the planes E1, E2, the glass body 20, which surrounds the electrodes 19, tapers, with the tapered ends of the glass body 20 in particular bearing the pins 21 for establishing electrical contact with the electrodes 19. Physically, therefore, the electrodes 19 preferably lie largely outside of the cooling region B of the cooling system or blower air system 13. This embodiment is particularly preferably used in medium-format machines, such as sheet-fed printing presses. Medium format machines can be used to process processing material measuring at least approximately 1 m in width, for example.
Regarding the mode of operation: In order for the radiation source, in particular a UV emitter 2, to also be cooled well on its underside, air is preferably blown in on both sides, in particular beyond the irradiation range of the UV module 1. This air preferably meets at the center beneath the UV module 1, in particular approximately at the center of the UV emitter 2. The inflowing ambient air constricted by the blower air jets 17 in the UV module 1 is transported to the underside of the UV emitter 2. In this way, the underside of the UV emitter 2 is intensely cooled. Furthermore, cooling becomes more turbulent overall and the upper side of the UV emitter 2 is also cooled better. WALTER
The additional air is preferably introduced or blown in exclusively between electrodes 19 of the UV emitter 2 or over the length of the UV module 1. This can be accomplished by means of plates and/or blower air nozzles.
The air that is preferably introduced or blown in on both sides can be either a partial volume or at least nearly all of the cooling air acting in the UV module 1. Preferably, however, 80% to 50% of the cooling air is formed by the inflowing ambient air flow 11, and 20% to 50% of the cooling air is formed by the air introduced by the blower air system 13. In particular, a proportion of 1/3 of the air or blower air 17 that is additionally introduced by the blower air system 13, and a proportion of 2/3 of the inflowing ambient air flow 11 is sought.
For example, the UV emitter 2 can be operated at an output of between approx. 80 W/cm and approx. 200 W/cm. The blower air system 13 can also be activated or switched on dependent on the output. In particular, the blower air system 13 can be activated only after it reaches an average output, for example at approximately 120 to 140 W/cm. In that case, the blower air system 13 can be fully inactive or can be fully deactivated below an emitter output of, for example, 120 to 140 W/cm. For example, the blower air system 13 can be activated as soon as it reaches 120 to 140 W/cm. Preferably, the effect of the blower air system 13 can be increased as the emitter output increases. In particular, the blower air system 13 can begin to operate as soon as an emitter output of 120 to 140 W/cm is reached and can preferably be increased linearly or in a functionally dependent manner up to a maximum emitter output of 200 W/cm, so that at an emitter output of 200 W/cm, the blower air system 13 is operating at 100% output.
In the case of functionally dependent control, the blower air can be adjusted in particular according to a set of characteristics, which can have local maxima and/or minima, for example. In that case, the blower air can be adjusted on the basis of a curve established, for example, between 120 W/cm and 200 W/cm. A function for operating the blower air system 13 can be specified and/or modified based on the emitter output, in particular dependent on the machine. However, the effect of the blower air system 13 can also be adjusted individually and/or can also be embodied as controlled or regulated, for example, according to the emitter output. In that case, the current emitter output can be known to a control device, in particular the machine controller, or can be determined by a sensor system. By reducing the effect of the blower air system 13 or by switching off the blower air system 13 at a low emitter output, for example below 140 W/cm, a blow-out of the UV emitter 2 is reliably prevented.
While a preferred embodiment of a processing machine having a radiation dryer and a method for operating such a dryer is disclosed fully and completely hereinabove, it will be apparent to one of skill in the art that various changes can be made thereto, without departing from the true spirit and scope of the present invention, which is accordingly to be limited only by the appended claims.
Number | Date | Country | Kind |
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10 2018 206 154.8 | Apr 2018 | DE | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2019/059858 | 4/16/2019 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2019/201960 | 10/24/2019 | WO | A |
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Number | Date | Country | |
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20210001621 A1 | Jan 2021 | US |