EP0481554A1 - Central device for distribution, recirculation and evacuation of air - Google Patents

Central device for distribution, recirculation and evacuation of air Download PDF

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Publication number
EP0481554A1
EP0481554A1 EP91202625A EP91202625A EP0481554A1 EP 0481554 A1 EP0481554 A1 EP 0481554A1 EP 91202625 A EP91202625 A EP 91202625A EP 91202625 A EP91202625 A EP 91202625A EP 0481554 A1 EP0481554 A1 EP 0481554A1
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EP
European Patent Office
Prior art keywords
air
evacuation
mixture
manifold
pipe
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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.)
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EP91202625A
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German (de)
French (fr)
Inventor
Paolo Rivera
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ROTOMEC - Costruzioni Meccaniche Elettriche - SpA
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ROTOMEC - Costruzioni Meccaniche Elettriche - SpA
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Publication of EP0481554A1 publication Critical patent/EP0481554A1/en
Withdrawn legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41FPRINTING MACHINES OR PRESSES
    • B41F23/00Devices for treating the surfaces of sheets, webs, or other articles in connection with printing
    • B41F23/04Devices for treating the surfaces of sheets, webs, or other articles in connection with printing by heat drying, by cooling, by applying powders
    • B41F23/0403Drying webs
    • B41F23/0423Drying webs by convection
    • B41F23/0426Drying webs by convection using heated air

Definitions

  • the subject of the present invention is a centralized device for the distribution, recirculation and evacuation of air intended to produce the evaporation of a vehicle in user equipment, such as sections of machines for rotogravure printing, processing machines and the like.
  • the different colors of a subject are printed one after the other on a support in successive sections of the machine, the number of which can vary, for example, from three to ten or more.
  • the ink or lacquer used for printing must be diluted by means of a vehicle, usually a solvent, the purpose of which is to give the ink or lacquer an appropriate viscosity and to allow, in the printing, the desired color tone.
  • This vehicle must be removed by evaporation after the printing of each color, before going on to printing the successive color.
  • the printing machine includes a number of evaporation tunnels, interposed between the different successive printing sections.
  • each evaporation tunnel a current of air is blown, through nozzles provided for this purpose, on the face of the support which has just been printed, in order to produce the evaporation of the vehicle, and the mixture of air and vapor that forms this way is exhausted from the tunnel.
  • the flow rate, speed and temperature of the air blown into each evaporation tunnel must be chosen in an appropriate manner, on one side to ensure complete evaporation of the vehicle during the period of permanence in the tunnel, and on the other hand so as to obtain an appropriate concentration of the vapor in the evacuated mixture.
  • the vehicle to be evaporated is a solvent which, with air, forms a flammable and, under certain conditions, detonating mixture. It is therefore necessary, for safety reasons, for the evacuated mixture to contain a lower vapor concentration, while respecting an appropriate safety coefficient, relative to the lower explosion limit of the mixture.
  • the prescriptions concerning the pollution of the environment do not allow to simply discharge into the atmosphere the mixtures of air and vehicle vapor evacuated from the tunnel, and therefore these mixtures must be conveyed to depuration devices. to recover the vehicle vapor contained therein, or else to destroy it, usually by combustion.
  • depuration devices to recover the vehicle vapor contained therein, or else to destroy it, usually by combustion.
  • the costs involved in the management of these depuration devices are all the greater the larger the quantities of mixture to be treated and the smaller the concentration of steam in these mixtures. It is therefore important that, while respecting the safety requirements, the concentration of the vapor in the treated mixture is set to the highest possible value.
  • each tunnel is provided with its own air distribution circuit, which is regulated, generally by hand, so that it can introduce, exhaust and recycle appropriate, regulated air flows. depending on the quality and quantity of vehicle to be evaporated in the tunnel in question.
  • the quantities of vehicle which must evaporate in the successive tunnels of the same machine for printing in rotogravure, during the printing of the same subject, can be very different, considering that the printed subject can have very different surfaces covered by the various colors, and this gives rise to correspondingly different amounts of vehicle to be evaporated in the different sections.
  • the object of the invention is to provide a device making it possible to distribute air to a number of user devices while respecting the different requirements of each of them but, at the same time, by centralizing control equipment intended to optimize the management of the entire system.
  • a device for the distribution, recirculation and evacuation of air with respect to user equipment each of which is provided with an air supply pipe, a fan, a discharge pipe and, if necessary, a heat exchanger
  • the device is centralized for a plurality of said devices and that it comprises a collector of discharge, connected to the air supply lines of the various apparatuses, a mixture suction manifold, connected to the evacuation lines of the various apparatuses, a fresh air suction line, a supply line to the exhaust, an exhaust fan inserted on said evacuation delivery pipe, a valve system comprising three valves inserted, respectively, between said mixture suction manifold and said evacuation delivery pipe, between said mixture suction manifold and said delivery manifold, and between said pure air suction pipe and said delivery manifold, at least one drive device arranged to control said valves, and a connected continuous analyzer to said mixture suction manifold and arranged to control said drive device.
  • the device according to the invention feeds partially recycled air, through its delivery manifold, to a plurality of devices, each of which uses the air supplied by means of its own fan, adjusted according to requirements. particular of the apparatus itself, and if necessary by heating this air by means of its own heat exchanger, also adjusted according to the particular requirements of the apparatus considered, and the mixture of air and vapor evacuated by the various switchgear is resembled by the mixture suction collector, mixing it with the mixture discharged by the other connected switchgear; this resulting mixture is analyzed to establish the concentration of the vehicle contained therein, and the three valves of the valve system are adjusted by their driving device, under the control of the analyzer, so as to route to the evacuation, under the action of the exhaust fan, a fraction of this mixture, to recycle a fraction of this mixture by routing it to the discharge manifold, and to add to this recycled fraction of mixture a certain amount of pure air from of the fresh air suction line.
  • this process is monitored by a continuous analyzer, it can take place in such a way as to meet safety requirements and, at the same time, to adjust the concentration of the vapor in the mixture sent to the discharge to the most suitable value. , and therefore the recovery or destruction of the vapor contained.
  • the advantages of using a device according to the invention are numerous.
  • the device serves a number of devices, and therefore the installation and management costs are much lower than for a plurality of similar devices arranged to each serve only one device. No air adjustment is no longer necessary in single groups.
  • the device ensures the delivery to the evacuation of the smallest possible quantities of mixture, containing the greatest possible vapor concentration, thus making it possible to reduce the costs of installation and management of the depuration device.
  • the various characteristics of the mixtures discharged by the various devices are brought to average values by the reciprocal mixture, so that the mixtures with a lower vapor content serve to dilute the more concentrated mixtures, and vice versa.
  • the recirculation of the air and steam mixture can be kept at the highest value compatible with the operating conditions and with the safety requirements.
  • the device further comprises a pressure sensor connected to the mixture suction manifold and arranged to control the operation of the exhaust fan.
  • a second continuous analyzer is connected to the discharge collector in order to allow a control of the regular operation of the device.
  • a heat exchanger is arranged to operate between the evacuation supply line and the pure air suction line, with the aim of preheating the pure air drawn in at the expense of the heat of the mixture supplied to evacuation.
  • the device according to the invention can control, for example, the distribution of air to all the sections of one or more machines for rotogravure printing, or else two or more devices according to the invention can be provided, each of which is connected to a plurality of sections of the apparatus, having requirements compatible with each other but not compatible with the requirements of other sections of apparatus.
  • Each of the squares distinguished by the letters A, B, C, (D), ... represents the solvent removal device forming part of a section of a machine for rotogravure printing.
  • the number of these sections can be any.
  • Each solvent removal device comprises a tunnel 1 (well known per se and which will not be described), through which the printed support which is to be dried is passed by evaporating the vehicle or solvent from the ink or the lacquer applied to the support.
  • a tunnel (well known per se and which will not be described), through which the printed support which is to be dried is passed by evaporating the vehicle or solvent from the ink or the lacquer applied to the support.
  • an air current is blown coming from an air supply pipe 6, by means of nozzle systems, which are also well known and which do not are not shown, actuated by an electric fan 8 intended to be adjusted locally according to the particular requirements of the section considered.
  • the supply air can be heated by means of a heat exchanger 7, which is also locally adjusted according to the particular requirements of the section in question.
  • the mixture of air and solvent vapor is carried out of the tunnel 1 by means of an evacuation pipe 9.
  • these components are substantially those of a usual device for removing the solvent, intended to suck in water. air from the medium and to discharge into the medium a mixture of air and vapor of solvent, as it could be used before the adoption of prescriptions relating to protection against pollution of the medium.
  • each section also comprises an inlet valve 2, inserted on the air supply line 6, and an outlet valve 3, inserted on the discharge line 9, and these valves 2 and 3 are intended to be closed, thus isolating the section considered, when the latter is to remain inactive.
  • the air supply lines 6 of several sections are connected, upstream of the respective isolation valves 2, to a discharge manifold 4 of the device according to the invention.
  • all the discharge lines 9 of the same sections are connected, downstream of the respective isolation valves 3, to a manifold 5 for mixing suction of the device according to the invention.
  • the mixture suction manifold 5 is connected to an inlet I of a valve body 14, and in a similar manner the discharge manifold 4 is connected to an outlet Il of the valve body 14.
  • the valve body 14 is provided with another outlet III, which is connected, via a line 21, an electric exhaust fan 10 and, if necessary, a heat exchanger 22, to a depuration device 23.
  • the depuration device 23 can operate by recovering the vapor contained in the mixture it receives, or else by destroying this vapor. In any case, it routes purified air to an outlet 24, which can be discharged into the medium.
  • the valve body 14 is also provided with an inlet IV for clean air coming via a line 20 and, if necessary, the heat exchanger 22, with an air intake 26 which can be opened in the middle.
  • the operation of the exhaust electric fan 10 is preferably controlled, according to actual need, by a pressometric sensor 12 connected to the mixture suction manifold 5. This is specially used to proportion the operation of the device to variations in the flow rate of the mixture sucked in by the manifold 5, also taking into account the fact that a variable number of sections of the apparatus served may be inactive and therefore have been isolated by means of the corresponding valves 2 and 3.
  • the electric fan 10 must always maintain a certain degree of vacuum in the mixture suction manifold 5, and therefore in the tunnels 1, in order to prevent the escape of solvent vapors from the tunnels; as a consequence of this depression, a certain amount of air (called “false air”) is sucked into the tunnels 1, as indicated diagrammatically by the arrows 11, through the openings provided for the entry and the exit of the support to be treated .
  • Other air can also be sucked around the printing units of the machine in order to prevent small amounts of solvent, released from the containers applied to these groups, being introduced into the medium.
  • the flow passing through the mixture suction manifold 5 is always somewhat greater than the flow passing through the discharge manifold 4.
  • valve body 14 In the valve body 14 are installed three valves: a discharge valve 15, arranged between the inlet 1 for mixing suction and the outlet III for delivery to the discharge, a valve 16 for clean air, arranged between the inlet IV for clean air and the outlet outlet Il, and a recirculation valve 17, disposed between the inlet 1 for mixing suction and the outlet outlet Il.
  • a discharge valve 15 arranged between the inlet 1 for mixing suction and the outlet III for delivery to the discharge
  • valve 16 for clean air arranged between the inlet IV for clean air and the outlet outlet Il
  • a recirculation valve 17 disposed between the inlet 1 for mixing suction and the outlet outlet Il.
  • the valves 15 to 17 can each be controlled by its own drive device, but preferably, as in the example shown, they are controlled collectively by a common drive device 18, for example pneumatic.
  • the valve drive device is controlled by a continuous analyzer 13, inserted on the mixture suction manifold 5, this analyzer being constituted by an apparatus known per se, capable of determining the concentration of the vapor of solvent in the mixture passing through the collector 5, or else the lower explosion limit of the mixture.
  • the signal produced by this analyzer is received by a computer 27 and, under the control of this computer, the drive device 18 moves the valves 15 to 17 to determine said subdivision of the flow of incoming air and vapor mixture, as well as the addition of pure air, so as to tend towards the achievement of optimal operating conditions.
  • a second analyzer 19 can be conveniently inserted on the discharge collector 4. It has no control functions on the device, but it allows an advantageous verification of the correct functioning of the device.
  • the operation of the device is as follows. At the beginning of the operation, of course, the concentration of the vapor contained in the mixture sucked by the manifold 5 is reduced.
  • the analyzer 13 detects this reduced concentration and therefore the computer 27, through the drive device 18, regulates the valves 15 to 17 by giving the valves 15 and 16 the minimum opening and the valve 17 l maximum opening, so that the maximum percentage of the mixture coming from the manifold 5, admitted for recirculation, is conveyed to the discharge manifold 4, while the smallest possible quantity of this mixture is conveyed to the evacuation via line 21 , and the smallest possible quantity of pure air is introduced via line 20.
  • the concentration of the solvent vapor in the mixture passing through the manifold 5 gradually increases. If, and when, as a result of this increase, the concentration of vapor in the mixture reaches a preset limit value, detected by the analyzer 13, the computer 27 controls the drive device 18 to move the valves 15 to 17 , and more precisely by opening valves 15 and 16 further and closing valve 17 more, so as to reduce the percentage of mixture which will recirculate and increase the percentage of mixture which is conveyed to the evacuation and the quantity of fresh air added.
  • the analyzer 13, the computer 27 and the drive device 18 continuously keep the valves 15 to 17 under control, increasing or reducing, as appropriate, the percentage of mixture that is recirculated , so as to maintain the concentration of the vapor in the mixture which is supplied to the depuration device 23 near the optimum preset value.
  • the device according to the invention makes it possible to be as close as possible to the optimal conditions, insofar as the operating conditions and the pre-established safety requirements allow, the mixture of air and steam supplied to the depuration, while allowing local, separate and independent adjustment of the operating conditions in each of the devices served.
  • the depuration device 23 is not a part of the device according to the invention; it can be of any known genus and will not be described.
  • the heat exchanger 22 makes it possible to recover part of the heat possessed by the mixture conveyed to the evacuation, by transferring this heat to the pure air sucked in. However, this is not always advantageous, and therefore the heat exchanger 22 should not be considered as a necessary element of the device according to the invention.
  • part of the purified air, discharged into the atmosphere through the outlet 24 can be routed via a connection 25 to the pipe 26 for the entry of clean air, thus achieving a partially closed circuit.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Treating Waste Gases (AREA)
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  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)

Abstract

A central device for the distribution, recirculation and evacuation of air with respect to a plurality of using equipments (A, B, C, D,...), each of which is provided with an air supply pipe (6), a fan (8), an evacuation pipe (9) and, if necessary, a heat exchanger (7), this device comprising a delivery manifold (4), connected to the air supply pipes (6) of the various equipments, a mixture intake manifold (5), connected to the evacuation pipes (9) of the various equipments, a pure air intake pipe (20), an evacuation routing pipe (21), an evacuation fan (10) inserted in this evacuation routing pipe, a valve block (14) comprising three valves (15, 17, 16) inserted, respectively, between the mixture intake manifold (5) and the evacuation routing pipe (21), between the mixture intake manifold (5) and the delivery manifold (4) and between the pure air intake pipe (20) and the delivery manifold (4), at least one driving device (18) disposed for controlling the said valves, and a continuous analyser (13) connected to the mixture intake manifold (5) and disposed to control the driving device (18) by the intermediary of a computer (23) <IMAGE>

Description

La présente invention a pour objet un dispositif centralisé pour la distribution, la recirculation et l'évacuation d'air destiné à produire l'évaporation d'un véhicule dans des appareillages utilisateurs, tels que des sections de machines pour l'impression en rotogravure, de machines de transformation et similaires.The subject of the present invention is a centralized device for the distribution, recirculation and evacuation of air intended to produce the evaporation of a vehicle in user equipment, such as sections of machines for rotogravure printing, processing machines and the like.

L'invention sera expliquée en faisant référence particulière aux machines pour l'impression en rotogravure, qui en forment une application caractéristique, mais il doit être bien entendu que cette application particulière ne pose aucunement une limite pour l'application plus générale de l'invention.The invention will be explained with particular reference to machines for rotogravure printing, which form a characteristic application, but it should be understood that this particular application in no way poses a limit for the more general application of the invention .

Dans les machines pour l'impression en rotogravure, les différentes couleurs d'un sujet sont imprimées l'une après l'autre sur un support en des sections successives de la machine, dont le nombre peut varier, par exemple, de trois à dix ou davantage. L'encre ou la laque utilisés pour l'impression doivent être dilués moyennant un véhicule, d'habitude un solvant, dont le but est de conférer à l'encre ou à la laque une viscosité appropriée et de permettre d'atteindre, dans l'impression, la tonalité de couleur désirée. Ce véhicule doit être emporté par évaporation après l'impression de chaque couleur, avant de passer à l'impression de la couleur successive. Pour effectuer cette opération, la machine d'impression comprend nombre de tunnels d'évaporation, interposés entre les différentes sections d'impression successives. Dans chaque tunnel d'évaporation, un courant d'air est soufflé, par des tuyères prévues à cet effet, sur la face du support qu'on vient d'imprimer, afin de produire l'évaporation du véhicule, et le mélange d'air et de vapeur qui se forme de cette façon est évacué du tunnel.In machines for rotogravure printing, the different colors of a subject are printed one after the other on a support in successive sections of the machine, the number of which can vary, for example, from three to ten or more. The ink or lacquer used for printing must be diluted by means of a vehicle, usually a solvent, the purpose of which is to give the ink or lacquer an appropriate viscosity and to allow, in the printing, the desired color tone. This vehicle must be removed by evaporation after the printing of each color, before going on to printing the successive color. To perform this operation, the printing machine includes a number of evaporation tunnels, interposed between the different successive printing sections. In each evaporation tunnel, a current of air is blown, through nozzles provided for this purpose, on the face of the support which has just been printed, in order to produce the evaporation of the vehicle, and the mixture of air and vapor that forms this way is exhausted from the tunnel.

Le débit, la vitesse et la température de l'air soufflé dans chaque tunnel d'évaporation doivent être choisis d'une façon appropriée, d'un côté pour assurer l'évaporation complète du véhicule pendant la période de permanence dans le tunnel, et d'autre côté de sorte à obtenir une concentration appropriée de la vapeur dans le mélange évacué. Dans la plupart des cas le véhicule à évaporer est un solvant qui forme avec l'air un mélange inflammable et, en certaines conditions, détonant. Il est donc nécessaire, pour des raisons de sûreté, que le mélange évacué contienne une concentration de vapeur plus réduite, en respectant une coefficient de sûreté approprié, par rapport à la limite inférieure d'explosion du mélange. D'autre côté, les prescriptions concernant la pollution du milieu ne permettent pas de décharger simplement dans l'atmosphère les mélanges d'air et de vapeur de véhicule évacués du tunnel, et de ce fait ces mélanges doivent être acheminés à des dispositifs de dépuration pour en récupérer la vapeur de véhicule qui y est contenue, ou bien pour la détruire, d'habitude par combustion. Les frais comportés par la gestion de ces dispositifs de dépuration sont d'autant plus grands que sont grandes les quantités de mélange à traiter et qu'est petite la concentration de la vapeur dans ces mélanges. De ce fait il est important que, tout en respectant les exigences de sûreté, la concentration de la vapeur dans le mélange traité soit réglée à la valeur la plus haute possible.The flow rate, speed and temperature of the air blown into each evaporation tunnel must be chosen in an appropriate manner, on one side to ensure complete evaporation of the vehicle during the period of permanence in the tunnel, and on the other hand so as to obtain an appropriate concentration of the vapor in the evacuated mixture. In most cases the vehicle to be evaporated is a solvent which, with air, forms a flammable and, under certain conditions, detonating mixture. It is therefore necessary, for safety reasons, for the evacuated mixture to contain a lower vapor concentration, while respecting an appropriate safety coefficient, relative to the lower explosion limit of the mixture. On the other hand, the prescriptions concerning the pollution of the environment do not allow to simply discharge into the atmosphere the mixtures of air and vehicle vapor evacuated from the tunnel, and therefore these mixtures must be conveyed to depuration devices. to recover the vehicle vapor contained therein, or else to destroy it, usually by combustion. The costs involved in the management of these depuration devices are all the greater the larger the quantities of mixture to be treated and the smaller the concentration of steam in these mixtures. It is therefore important that, while respecting the safety requirements, the concentration of the vapor in the treated mixture is set to the highest possible value.

Pour satisfaire à ces exigences, chaque tunnel est pourvu d'un propre circuit de distribution d'air, qui est réglé, en général à la main, de sorte qu'il puisse introduire, évacuer et recycler des débits d'air appropriés, réglés en fonction de la qualité et quantité de véhicule qu'on doit faire évaporer dans le tunnel considéré. Les quantités de véhicule qui doivent évaporer dans les tunnels successifs d'une même machine pour l'impression en rotogravure, pendant l'impression d'un même sujet, peuvent être très différentes, en considérant que le sujet imprimé peut présenter des surfaces très différentes couvertes par les divers couleurs, et cela donne lieu à des quantités correspondamment différentes de véhicule à faire évap rer dans les différentes sections. Toutefois, les conditions optimales peuvent être atteintes seulement avec une faible approximation par un réglage à la main des circuits de distribution, tandis qu'un réglage des circuits de distribution singuliers, contrôlé par des appareils automatiques évolués, serait excessivement coûteuse en vue du nombre de tunnels présents dans une machine pour l'impression en rotogravure. On ne peut pas penser à un circuit de distribution unique qui fait fonctionner tous les tunnels sans différences, du fait des exigences, qui peuvent aussi être très différentes, qui se présentent dans les différentes sections de la machine.To meet these requirements, each tunnel is provided with its own air distribution circuit, which is regulated, generally by hand, so that it can introduce, exhaust and recycle appropriate, regulated air flows. depending on the quality and quantity of vehicle to be evaporated in the tunnel in question. The quantities of vehicle which must evaporate in the successive tunnels of the same machine for printing in rotogravure, during the printing of the same subject, can be very different, considering that the printed subject can have very different surfaces covered by the various colors, and this gives rise to correspondingly different amounts of vehicle to be evaporated in the different sections. However, optimal conditions can only be achieved with a small approximation by manual adjustment of the distribution circuits, while adjustment of the individual distribution circuits, controlled by advanced automatic devices, would be excessively expensive in view of the number of tunnels present in a machine for rotogravure printing. We cannot think of a single distribution circuit which operates all the tunnels without differences, due to the requirements, which can also be very different, which arise in the different sections of the machine.

Comme on l'a déjà dit, les exigences particulières indiquées pour les machines d'impression en rotogravure, ou bien des exigences similaires, sont rencontrées aussi en d'autres appareillages, comme les machines de transformation et autres.As already mentioned, the particular requirements indicated for rotogravure printing machines, or similar requirements, are also met in other equipment, such as processing machines and the like.

En vue de ces problèmes, le but de l'invention est de réaliser un dispositif permettant d'effectuer une distribution d'air à nombre d'appareillages utilisateurs en respectant les différentes exigences de chacun d'entr'eux mais, en même temps, en centralisant les appareillages de contrôle destinés à rendre optimale la gestion du système tout entier.In view of these problems, the object of the invention is to provide a device making it possible to distribute air to a number of user devices while respecting the different requirements of each of them but, at the same time, by centralizing control equipment intended to optimize the management of the entire system.

Ce but est atteint, suivant l'invention, moyennant un dispositif pour la distribution, la recirculation et l'évacuation d'air par rapport à des appareillages utilisateurs, chacun desquels est pourvu d'une conduite d'alimentation d'air, d'un ventilateur, d'une conduite d'évacuation et, le cas échéant, d'un échangeur de chaleur, caractérisé en ce que le dispositif est centralisé pour une pluralité desdits appareillages et qu'il comprend un collecteur de refoulement, connecté aux conduites d'alimentation d'air des diverses appareillages, un collecteur d'aspiration de mélange, connecté aux conduites d'évacuation des diverses appareillages, une conduite d'aspiration d'air pur, une conduite d'acheminement à l'évacuation, un ventilateur d'évacuation inséré sur ladite conduite d'acheminement à l'évacuation, un système de soupapes comprenant trois soupapes insérées, respectivement, entre ledit collecteur d'aspiration de mélange et ladite conduite d'acheminement à l'evacuation, entre ledit collecteur d'aspiration de mélange et ledit collecteur de refoulement, et entre ladite conduite d'aspiration d'air pur et ledit collecteur de refoulement, au moins un dispositif d'entraînement disposé pour commander lesdites soupapes, et un analyseur en continu connecté audit collecteur d'aspiration de mélange et disposé pour contrôler ledit dispositif d'entraînement.This object is achieved, according to the invention, by means of a device for the distribution, recirculation and evacuation of air with respect to user equipment, each of which is provided with an air supply pipe, a fan, a discharge pipe and, if necessary, a heat exchanger, characterized in that the device is centralized for a plurality of said devices and that it comprises a collector of discharge, connected to the air supply lines of the various apparatuses, a mixture suction manifold, connected to the evacuation lines of the various apparatuses, a fresh air suction line, a supply line to the exhaust, an exhaust fan inserted on said evacuation delivery pipe, a valve system comprising three valves inserted, respectively, between said mixture suction manifold and said evacuation delivery pipe, between said mixture suction manifold and said delivery manifold, and between said pure air suction pipe and said delivery manifold, at least one drive device arranged to control said valves, and a connected continuous analyzer to said mixture suction manifold and arranged to control said drive device.

En vue de ces caractéristiques, le dispositif suivant l'invention alimente de l'air partiellement recyclé, à travers son collecteur de refoulement, à une pluralité d'appareillages, chacun desquels utilise l'air alimenté moyennant son propre ventilateur, réglé suivant les exigences particulières de l'appareillage lui-même, et le cas échéant en rechauffant cet air moyennant son propre échangeur de chaleur, réglé lui-aussi suivant les exigences particulières de l'appareillage considéré, et le mélange d'air et vapeur évacué par les divers appareillages est ressemblé par le collecteur d'aspiration de mélange, en le mêlant avec le mélange évacué par les autres appareillages connectés; ce mélange résultant est analysé pour établir la concentration du véhicule qui y est contenu, et les trois soupapes du système de soupapes sont réglées par leur dispositif d'entraînement, sous le contrôle de l'analyseur, de sorte à acheminer à l'évacuation, sous l'action du ventilateur d'évacuation, une fraction de ce mélange, de recycler une fraction de ce mélange en l'acheminant au collecteur de refoulement, et d'additionner à cette fraction recyclée de mélange une certaine quantité d'air pur provenant de la conduite d'aspiration d'air pur. Ce processus étant contrôlé par un analyseur en continu, il peut avoir lieu de sorte à respecter les exigences de sûreté et, en même temps, à régler à la valeur la plus convenable possible la concentration de la vapeur dans le mélange acheminé à l'évacuation, et donc à la récupération ou bien à la destruction de la vapeur contenue.In view of these characteristics, the device according to the invention feeds partially recycled air, through its delivery manifold, to a plurality of devices, each of which uses the air supplied by means of its own fan, adjusted according to requirements. particular of the apparatus itself, and if necessary by heating this air by means of its own heat exchanger, also adjusted according to the particular requirements of the apparatus considered, and the mixture of air and vapor evacuated by the various switchgear is resembled by the mixture suction collector, mixing it with the mixture discharged by the other connected switchgear; this resulting mixture is analyzed to establish the concentration of the vehicle contained therein, and the three valves of the valve system are adjusted by their driving device, under the control of the analyzer, so as to route to the evacuation, under the action of the exhaust fan, a fraction of this mixture, to recycle a fraction of this mixture by routing it to the discharge manifold, and to add to this recycled fraction of mixture a certain amount of pure air from of the fresh air suction line. Since this process is monitored by a continuous analyzer, it can take place in such a way as to meet safety requirements and, at the same time, to adjust the concentration of the vapor in the mixture sent to the discharge to the most suitable value. , and therefore the recovery or destruction of the vapor contained.

Les avantages de l'emploi d'un dispositif suivant l'invention sont nombreux. Le dispositif dessert nombre d'appareillages, et donc les frais d'installation et de gestion sont bien plus réduits que pour une pluralité de dispositifs similaires disposés pour desservir chacun un appareillage seulement. Aucun réglage de l'air n'est plus nécessaire dans les groupes singuliers. Le dispositif assure l'acheminement à l'évacuation des quantités les plus petites possibles de mélange, contenant la concentration de vapeur la plus grande possible, ainsi permettant de réduire les frais d'installation et de gestion du dispositif de dépuration. Les diverses caractéristiques des mélanges évacués par les différents appareillages sont portées à des valeurs moyennes par le mélange réciproque, de sorte que les mélanges dont le contenu de vapeur est plus réduit servent à diluer les mélanges plus concentrées, et vice-versa. La recirculation du mélange d'air et vapeur peut être tenue à la valeur la plus élevée compatible avec les conditions d'exercice et avec les exigences de sûreté. On assure toujours un équilibre entre les collecteurs d'aspiration de mélange et de refoulement, connectés aux divers appareillages. De plus, toutes ces caractéristiques sont obtenues en travaillant avantageusement sur un mélange de propriétés moyennes, tout en assurant la possibilité de réaliser dans chaque appareillage les conditions locales optimales en vue de ses exigences particulières de fonctionnement.The advantages of using a device according to the invention are numerous. The device serves a number of devices, and therefore the installation and management costs are much lower than for a plurality of similar devices arranged to each serve only one device. No air adjustment is no longer necessary in single groups. The device ensures the delivery to the evacuation of the smallest possible quantities of mixture, containing the greatest possible vapor concentration, thus making it possible to reduce the costs of installation and management of the depuration device. The various characteristics of the mixtures discharged by the various devices are brought to average values by the reciprocal mixture, so that the mixtures with a lower vapor content serve to dilute the more concentrated mixtures, and vice versa. The recirculation of the air and steam mixture can be kept at the highest value compatible with the operating conditions and with the safety requirements. A balance is always ensured between the mixture suction and discharge collectors, connected to the various devices. In addition, all these characteristics are obtained by working advantageously on a mixture of average properties, while ensuring the possibility of achieving in each apparatus the optimum local conditions for its particular operating requirements.

De préférence le dispositif comprend en outre un capteur pressométrique connecté au collecteur d'aspiration de mélange et disposé pour contrôler le fonctionnement du ventilateur d'évacuation. De préférence, un deuxième analyseur en continu est connecté au collecteur de refoulement à l'effet de permettre un contrôle du fonctionnement régulier du dispositif. De préférence un échangeur de chaleur est disposé pour opérer entre la conduite d' acheminement à l'évacuation et la conduite d'aspiration d'air pur, dans le but de préréchauffer l'air pur aspiré aux dépenses de la chaleur du mélange acheminé à l'évacuation. Enfin, compte tenu di fait qu'au dispositif doit être connecté un dispositif de dépuration du mélange acheminé à l'évacuation, on peut établir une connexion entre la sortie de ce dispositif de dépuration et l'entrée pour l'air pur aspiré, ainsi réalisant un circuit d'air partiellement fermé.Preferably the device further comprises a pressure sensor connected to the mixture suction manifold and arranged to control the operation of the exhaust fan. Preferably, a second continuous analyzer is connected to the discharge collector in order to allow a control of the regular operation of the device. Preferably, a heat exchanger is arranged to operate between the evacuation supply line and the pure air suction line, with the aim of preheating the pure air drawn in at the expense of the heat of the mixture supplied to evacuation. Finally, taking into account the fact that a device for purifying the mixture sent to the evacuation must be connected, a connection can be established between the outlet of this depuration device and the inlet for the pure air drawn in, thus achieving a partially closed air circuit.

Le dispositif suivant l'invention peut contrôler, par exemple, la distribution de l'air à toutes les sections d'une ou plusieurs machines pour l'impression en rotogravure, ou bien on peut prévoir deux ou plusieurs dispositifs suivant l'invention, chacun desquels est connecté à une pluralité de sections de l'appareillage, ayant des exigences compatibles entr'elles mais non compatibles avec les exigences d'autres sections d'appareillages.The device according to the invention can control, for example, the distribution of air to all the sections of one or more machines for rotogravure printing, or else two or more devices according to the invention can be provided, each of which is connected to a plurality of sections of the apparatus, having requirements compatible with each other but not compatible with the requirements of other sections of apparatus.

L'invention sera expliquée plus en détail en faisant référence à un mode de réalisation de l'invention, préféré mais qui doit être considéré comme un exemple non limitatif, appliqué à une machine pour l'impression en rotogravure. La seule figure du dessin annexé montre le schéma simplifié de l'appareillage et du dispositif suivant l'invention, avec le système de soupapes montré en section.The invention will be explained in more detail with reference to an embodiment of the invention, preferred but which should be considered as a non-limiting example, applied to a machine for printing in rotogravure. The only figure in the appended drawing shows the simplified diagram of the apparatus and the device according to the invention, with the valve system shown in section.

Chacun des carrés distingués par les lettres A, B, C, (D), ... représente le dispositif d'élimination du solvant faisant partie d'une section d'une machine pour l'impression en rotogravure. Le nombre de ces sections peut être quelconque. Chaque dispositif d'élimination du solvant comprend un tunnel 1 (bien connu en soi et qui ne sera pas décrit), à travers lequel on fait passer le support imprimé qui doit être séché en faisant évaporer le véhicule ou solvant de l'encre ou de la laque appliqué sur le support. Dans ce tunnel, sur la partie du support qu'on vient d'imprimer est soufflé un courant d'air provenant d'une conduite d'alimentation d'air 6, moyennant des systèmes de tuyères, elles-aussi bien connues et qui ne sont pas représentées, actionnées par un électroventilateur 8 destiné à être réglé localement en fonction des exigences particulières de la section considérée. De plus, l'air soufflé peut être réchauffé moyennant un échangeur de chaleur 7, qui est réglé lui-aussi localement en fonction des exigences particulières de la section considérée. Le mélange d'air et de vapeur de solvant est emportée du tunnel 1 moyennant une conduite d'évacuation 9. Comme on peut le remarquer, ces composants sont substantiellement ceux d'un dispositif habituel d'élimination du solvant, destiné à aspirer de l'air du milieu et à évacuer dans le milieu un mélange d'air et de vapeur de solvant, tel qu'il pouvait être employé avant qu'on adoptât des prescriptions relatives à la protection contre la pollution du milieu.Each of the squares distinguished by the letters A, B, C, (D), ... represents the solvent removal device forming part of a section of a machine for rotogravure printing. The number of these sections can be any. Each solvent removal device comprises a tunnel 1 (well known per se and which will not be described), through which the printed support which is to be dried is passed by evaporating the vehicle or solvent from the ink or the lacquer applied to the support. In this tunnel, on the part of the support which has just been printed, an air current is blown coming from an air supply pipe 6, by means of nozzle systems, which are also well known and which do not are not shown, actuated by an electric fan 8 intended to be adjusted locally according to the particular requirements of the section considered. In addition, the supply air can be heated by means of a heat exchanger 7, which is also locally adjusted according to the particular requirements of the section in question. The mixture of air and solvent vapor is carried out of the tunnel 1 by means of an evacuation pipe 9. As can be seen, these components are substantially those of a usual device for removing the solvent, intended to suck in water. air from the medium and to discharge into the medium a mixture of air and vapor of solvent, as it could be used before the adoption of prescriptions relating to protection against pollution of the medium.

Compte tenu du fait que certaines sections de l'appareillage peuvent rester inactives pendant certains travaux, chaque section comprend encore una soupape d'entrée 2, insérée sur la conduite d'alimentation d'air 6, et une soupape de sortie 3, insérée sur la conduite d'évacuation 9, et ces soupapes 2 et 3 sont destinées à être fermées, ainsi isolant la section considérée, lorsque celle-ci soit rester inactive.In view of the fact that certain sections of the apparatus may remain inactive during certain works, each section also comprises an inlet valve 2, inserted on the air supply line 6, and an outlet valve 3, inserted on the discharge line 9, and these valves 2 and 3 are intended to be closed, thus isolating the section considered, when the latter is to remain inactive.

Les conduites d'alimentation d'air 6 de plusieurs sections sont connectées, en amont des soupapes d'isolement 2 respectives, à un collecteur de refoulement 4 du dispositif suivant l'invention. D'une façon similaire, toutes les conduites d'évacuation 9 des mêmes sections sont connectées, en aval des soupapes d'isolement 3 respectives, à un collecteur 5 d'aspiration de mélange du dispositif suivant l'invention.The air supply lines 6 of several sections are connected, upstream of the respective isolation valves 2, to a discharge manifold 4 of the device according to the invention. Similarly, all the discharge lines 9 of the same sections are connected, downstream of the respective isolation valves 3, to a manifold 5 for mixing suction of the device according to the invention.

Le collecteur 5 d'aspiration de mélange est connecté à une entrée I d'un corps de soupapes 14, et d'une façon similaire le collecteur de refoulement 4 est connecté à une sortie Il du corps de soupapes 14. Le corps de soupapes 14 est pourvu d'une autre sortie III, laquelle est connectée, via une conduite 21, un ventilateur électrique d'évacuation 10 et, le cas échéant, un échangeur de chaleur 22, à un dispositif de dépuration 23. Le dispositif de dépuration 23 peut opérer par récupération de la vapeur contenue dans le mélange qu il reçoit, ou bien par destruction de cette vapeur. En tous cas il achemine à une sortie 24 de l'air dépuré, lequel peut être déchargé dans le milieu. Le corps de soupape 14 est encore pourvu d'une entrée IV pour de l'air pur provenant via une conduite 20 et, le cas échéant, l'échangeur de chaleur 22, d'une prise d'air 26 qui peut être ouverte dans le milieu. Toutefois il est aussi possible d'établir une connexion, indiquée en 25 par des lignes interrompues, entre la prise 26 et la sortie 24, de sorte à aspirer comme air pur une partie de l'air dépuré sortant du dispositif de dépuration 23. Dans ce cas le circuit de l'air est partiellement fermé. L'air pur aspiré, grâce à l'échangeur de chaleur 22, peut être préréchauffé aux dépenses de la chaleur du mélange d'air et de vapeur évacué; toutefois l'échangeur de chaleur 22 peut aussi être omis.The mixture suction manifold 5 is connected to an inlet I of a valve body 14, and in a similar manner the discharge manifold 4 is connected to an outlet Il of the valve body 14. The valve body 14 is provided with another outlet III, which is connected, via a line 21, an electric exhaust fan 10 and, if necessary, a heat exchanger 22, to a depuration device 23. The depuration device 23 can operate by recovering the vapor contained in the mixture it receives, or else by destroying this vapor. In any case, it routes purified air to an outlet 24, which can be discharged into the medium. The valve body 14 is also provided with an inlet IV for clean air coming via a line 20 and, if necessary, the heat exchanger 22, with an air intake 26 which can be opened in the middle. However, it is also possible to establish a connection, indicated at 25 by broken lines, between the outlet 26 and the outlet 24, so as to suck as pure air part of the purified air leaving the depuration device 23. In in this case the air circuit is partially closed. The pure air drawn in, thanks to the heat exchanger 22, can be preheated at the expense of the heat of the mixture of air and steam evacuated; however, the heat exchanger 22 can also be omitted.

Le fonctionnement de l'électroventilateur d'évacuation 10 est contrôlé, de préférence, en fonction de la nécessité réelle, par un capteur pressométrique 12 connecté au collecteur d'aspiration de mélange 5. Ce-la sert spécialement pour proportionner le fonctionnement du dispositif aux variations de débit du mélange aspiré par le collecteur 5, aussi en considération du fait qu'un nombre variable de sections des appareillages desservis peut être inactif et avoir donc été isolé moyennant les soupapes 2 et 3 correspondantes. L'électroventilateur 10 doit maintenir toujours un certain degré de dépression dans le collecteur d'aspiration de mélange 5, et donc dans les tunnels 1, à l'effet de prévenir la sortie de vapeurs de solvant des tunnels; comme conséquence de cette dépression, une certaine quantité d'air (dite "air faux") est aspiré dans les tunnels 1, comme indiqué schématiquement par les flèches 11, à travers les ouvertures prévues pour l'entrée et la sortie du support à traiter. De l'autre air peut être aussi aspiré autour des groupes d'impression de la machine afin d'éviter que des petites quantités de solvant, libérées des récipients appliqués à ces groupes, soient introduites dans le milieu. De ces faits, le débit parcourant le collecteur d'aspiration de mélange 5 est toujours quelque peu plus grand que le débit parcourant le collecteur de refoulement 4.The operation of the exhaust electric fan 10 is preferably controlled, according to actual need, by a pressometric sensor 12 connected to the mixture suction manifold 5. This is specially used to proportion the operation of the device to variations in the flow rate of the mixture sucked in by the manifold 5, also taking into account the fact that a variable number of sections of the apparatus served may be inactive and therefore have been isolated by means of the corresponding valves 2 and 3. The electric fan 10 must always maintain a certain degree of vacuum in the mixture suction manifold 5, and therefore in the tunnels 1, in order to prevent the escape of solvent vapors from the tunnels; as a consequence of this depression, a certain amount of air (called "false air") is sucked into the tunnels 1, as indicated diagrammatically by the arrows 11, through the openings provided for the entry and the exit of the support to be treated . Other air can also be sucked around the printing units of the machine in order to prevent small amounts of solvent, released from the containers applied to these groups, being introduced into the medium. As a result, the flow passing through the mixture suction manifold 5 is always somewhat greater than the flow passing through the discharge manifold 4.

Dans le corps de soupapes 14 sont installées trois soupapes: une soupape 15 d'évacuation, disposée entre l'entrée 1 d'aspiration de mélange et la sortie III d'acheminement à l'évacuation, une soupape 16 pour air pur, disposée entre l'entrée IV pour l'air pur et la sortie Il de refoulement, et une soupape 17 de recirculation, disposée entre l'entrée 1 d'aspiration de mélange et la sortie Il de refoulement. Ces soupapes, en fonction de leur position, produisent une subdivision du flux de mélange d'air et vapeur entrant par l'entrée 1 en un flux partiel de recirculation dirigé vers la sortie de refoulement II, et un flux partiel dirigé vers la sortie III pour être évacué, ainsi que l'addition audit flux de recirculation d'une certaine quantité d'air pur provenant de l'entrée IV et aussi dirigé vers la sortie Il de refoulement. Les soupapes 15 à 17 peuvent être contrôlées chacune par son propre dispositif d'entraînement, mais de préférence, comme dans l'exemple représenté, elles sont contrôlées collectivement par un dispositif commun d'entraînement 18, par exemple pneumatique. En tous cas le dispositif d'entraînement des soupapes est contrôlé par un analyseur en continu 13, inséré sur le collecteur 5 d'aspiration de mélange, cet analyseur étant constitué par un appareil connu en soi, capable de déterminer la concentration de la vapeur de solvant dans le mélange parcourant le collecteur 5, ou bien la limite inférieure d'explosion du mélange. Le signal produit par cet analyseur est reçu par un ordinateur 27 et, sous le contrôle de cet ordinateur, le dispositif d'entraînement 18 déplace les soupapes 15 à 17 pour déterminer ladite subdivision du flux de mélange d'air et vapeur entrant, ainsi que l'addition d'air pur, de sorte à tendre à la réalisation des conditions optimales de fonctionnement. En pratique on constate que, indépendamment de la concentration de la vapeur contenue, d'habitude il n'est pas à propos de faire recirculer plus que le 90% du mélange provenant du collecteur 5.In the valve body 14 are installed three valves: a discharge valve 15, arranged between the inlet 1 for mixing suction and the outlet III for delivery to the discharge, a valve 16 for clean air, arranged between the inlet IV for clean air and the outlet outlet Il, and a recirculation valve 17, disposed between the inlet 1 for mixing suction and the outlet outlet Il. These valves, depending on their position, produce a subdivision of the flow of mete lange of air and steam entering through inlet 1 in a partial recirculation flow directed towards the discharge outlet II, and a partial flow directed towards the outlet III to be evacuated, as well as the addition to said recirculation flow of a certain quantity of pure air coming from the IV inlet and also directed towards the discharge outlet II. The valves 15 to 17 can each be controlled by its own drive device, but preferably, as in the example shown, they are controlled collectively by a common drive device 18, for example pneumatic. In any case, the valve drive device is controlled by a continuous analyzer 13, inserted on the mixture suction manifold 5, this analyzer being constituted by an apparatus known per se, capable of determining the concentration of the vapor of solvent in the mixture passing through the collector 5, or else the lower explosion limit of the mixture. The signal produced by this analyzer is received by a computer 27 and, under the control of this computer, the drive device 18 moves the valves 15 to 17 to determine said subdivision of the flow of incoming air and vapor mixture, as well as the addition of pure air, so as to tend towards the achievement of optimal operating conditions. In practice, it can be seen that, independently of the concentration of the vapor contained, it is usually not advisable to recirculate more than 90% of the mixture coming from the collector 5.

Un deuxième analyseur 19 peut être opportunément inséré sur le collecteur de refoulement 4. Il n'a pas de fonctions de contrôle sur le dispositif, mais il autorise une vérification avantageuse du fonctionnement correct du dispositif.A second analyzer 19 can be conveniently inserted on the discharge collector 4. It has no control functions on the device, but it allows an advantageous verification of the correct functioning of the device.

Le fonctionnement du dispositif est le suivant. Au commencement du fonctionnement, bien entendu, la concentration de la vapeur contenue dans le mélange aspiré par le collecteur 5 est réduite. L'analyseur 13 détecte cette concentration réduite et par conséquent l'ordinateur 27, par l'entremise du dispositif d'entraînement 18, règle les soupapes 15 à 17 en donnant aux soupapes 15 et 16 l'ouverture minimale et à la soupape 17 l'ouverture maximale, de sorte que le pourcentage maximum du mélange provenant du collecteur 5, admis pour la recirculation, est acheminé au collecteur de refoulement 4, tandis que la plus petite quantité possible de ce mélange est acheminée à l'évacuation via la conduite 21, et la plus petite quantité possible d'air pur est introduite via la conduite 20. Se prolongeant le fonctionnement, en conséquence de la recirculation de mélange d'air et vapeur, la concentration de la vapeur de solvant dans le mélange parcourant le collecteur 5 augmente graduellement. Si, et lorsque, en conséquence de cette augmentation, la concentration de la vapeur dans le mélange atteint une valeur limite préétabli, détecté par l'analyseur 13, l'ordinateur 27 commande le dispositif d'entraînement 18 pour déplacer les soupapes 15 à 17, et plus précisement en ouvrant davantage les soupapes 15 et 16 et en fermant davantage la soupape 17, de sorte à réduire le pourcentage de mélange qui va recirculer et d'augmenter le pourcentage de mélange qui est acheminé à l'évacuation et la quantité d'air pur additionné. A partir de ce moment l'analyseur 13, l'ordinateur 27 et le dispositif d'entraînement 18 tiennent continuellement sous contrôle les soupapes 15 à 17, en augmentant ou réduisant, suivant l'opportunité, le pourcentage de mélange qu'on fait recirculer, de sorte à maintenir près de la valeur optimale préétablie la concentration de la vapeur dans le mélange qui est acheminé au dispositif de dépuration 23.The operation of the device is as follows. At the beginning of the operation, of course, the concentration of the vapor contained in the mixture sucked by the manifold 5 is reduced. The analyzer 13 detects this reduced concentration and therefore the computer 27, through the drive device 18, regulates the valves 15 to 17 by giving the valves 15 and 16 the minimum opening and the valve 17 l maximum opening, so that the maximum percentage of the mixture coming from the manifold 5, admitted for recirculation, is conveyed to the discharge manifold 4, while the smallest possible quantity of this mixture is conveyed to the evacuation via line 21 , and the smallest possible quantity of pure air is introduced via line 20. As operation continues, as a consequence of the recirculation of the air and vapor mixture, the concentration of the solvent vapor in the mixture passing through the manifold 5 gradually increases. If, and when, as a result of this increase, the concentration of vapor in the mixture reaches a preset limit value, detected by the analyzer 13, the computer 27 controls the drive device 18 to move the valves 15 to 17 , and more precisely by opening valves 15 and 16 further and closing valve 17 more, so as to reduce the percentage of mixture which will recirculate and increase the percentage of mixture which is conveyed to the evacuation and the quantity of fresh air added. From this moment the analyzer 13, the computer 27 and the drive device 18 continuously keep the valves 15 to 17 under control, increasing or reducing, as appropriate, the percentage of mixture that is recirculated , so as to maintain the concentration of the vapor in the mixture which is supplied to the depuration device 23 near the optimum preset value.

Le développement correct de l'opération d'évaporation dans les tunnels 1 est assuré par le fait que la concentration de la vapeur dans le mélange acheminé au collecteur de refoulement 4 est toujours inférieure de la concentration de la vapeur dans le mélange parcourant le collecteur 5, et cela soit dû à l'introduction de 1"'air faux" 11, soit dû à l'addition d'air pur provenant de la conduite 20.The correct development of the evaporation operation in the tunnels 1 is ensured by the fact that the concentration of the vapor in the mixture supplied to the delivery manifold 4 is always lower than the concentration of the vapor in the mixture passing through the manifold 5 , and this is either due to the introduction of "false air" 11, or due to the addition of pure air coming from line 20.

De cette façon le dispositif suivant l'invention permet d'avoisiner le plus possible aux conditions optimales, dans la mesure où l'autorisent les conditions de fonctionnement et les exigences de sûreté préétablies, le mélange d'air et vapeur acheminé à la dépuration, tout en autorisant un réglage local, séparé et indépendant, des conditions d'exercice dans chacun des appareillages desservis.In this way, the device according to the invention makes it possible to be as close as possible to the optimal conditions, insofar as the operating conditions and the pre-established safety requirements allow, the mixture of air and steam supplied to the depuration, while allowing local, separate and independent adjustment of the operating conditions in each of the devices served.

Le dispositif de dépuration 23 n'est pas une partie du dispositif suivant l'invention; il peut être de tout genre connu et il ne sera pas décrit. L'échangeur de chaleur 22 permet de récupérer une partie de la chaleur possédée par le mélange acheminé à l'évacuation, en transférant cette chaleur à l'air pur aspiré. Toutefois cela n'est pas toujours avantageux, et donc l'échangeur de chaleur 22 ne doit pas être considéré comme un élément nécessaire du dispositif suivant l'invention. Enfin, comme on l'a déjà remarqué, une partie de l'air dépuré, déchargé dans l'atmosphère par la sortie 24, peut être acheminée via une connection 25 à la conduite 26 d'entrée d'air pur, ainsi réalisant un circuit partiellement fermé.The depuration device 23 is not a part of the device according to the invention; it can be of any known genus and will not be described. The heat exchanger 22 makes it possible to recover part of the heat possessed by the mixture conveyed to the evacuation, by transferring this heat to the pure air sucked in. However, this is not always advantageous, and therefore the heat exchanger 22 should not be considered as a necessary element of the device according to the invention. Finally, as already noted, part of the purified air, discharged into the atmosphere through the outlet 24, can be routed via a connection 25 to the pipe 26 for the entry of clean air, thus achieving a partially closed circuit.

Des parties complémentaires différentes peuvent, bien entendu, être ajoutées au dispositif décrit, et diverses modifications, ainsi que tout remplacement par des équivalents techniques, peuvent être portées au dispositif décrit.Different complementary parts can, of course, be added to the device described, and various modifications, as well as any replacement by technical equivalents, can be made to the device described.

Claims (10)

1. Dispositif pour la distribution, la recirculation et l'évacuation d'air par rapport à des appareillages utilisateurs (A,B,C,D,...), chacun desquels est pourvu d'une conduite d'alimentation d'air (6), d'un ventilateur (8), d'une conduite d'évacuation (9) et, le cas échéant, d'un échangeur de chaleur (7), caractérisé en ce que le dispositif est centralisé pour une pluralité desdits appareillages et qu'il comprend un collecteur de refoulement (4), connecté aux conduites d'alimentation d'air (6) des diverses appareillages, un collecteur (5) d'aspiration de mélange, connecté aux conduites d'évacuation (9) des diverses appareillages, une conduite d'aspiration d'air pur (20), une conduite (21) d'acheminement à l'évacuation, un ventilateur d'évacuation (10) inséré sur ladite conduite (21) d'acheminement à l'évacuation, un système de soupapes (14) comprenant trois soupapes (15,17,16) insérées, respectivement, entre ledit collecteur (5) d'aspiration de mélange et ladite conduite (21) d'acheminement à l'evacuation, entre ledit collecteur (5) d'aspiration de mélange et ledit collecteur (4) de refoulement, et entre ladite conduite (20) d'aspiration d'air pur et ledit collecteur (4) de refoulement, au moins un dispositif d'entraînement (18) disposé pour commander lesdites soupapes, et un analyseur en continu (13) connecté audit collecteur (5) d'aspiration de mélange et disposé pour contrôler ledit dispositif d'entraînement (18).1. Device for the distribution, recirculation and evacuation of air in relation to equipment ges users (A, B, C, D, ...), each of which is provided with an air supply line (6), a fan (8), an exhaust line ( 9) and, where appropriate, a heat exchanger (7), characterized in that the device is centralized for a plurality of said devices and that it comprises a discharge manifold (4), connected to the supply lines of air (6) from the various devices, a manifold (5) for mixing suction, connected to the exhaust pipes (9) of the various devices, a pipe for suction of clean air (20), a pipe ( 21) for evacuation routing, an exhaust fan (10) inserted on said evacuation routing pipe (21), a valve system (14) comprising three valves (15,17,16) inserted, respectively, between said mixture suction manifold (5) and said evacuation delivery pipe (21), between said mixture suction manifold (5) and the edit delivery manifold (4), and between said clean air suction pipe (20) and said delivery manifold (4), at least one drive device (18) arranged to control said valves, and an analyzer continuously (13) connected to said mixture suction manifold (5) and arranged to control said drive device (18). 2. Dispositif suivant la revendication 1, caractérisé en ce qu'il comprend en outre un capteur pressométrique (12) connecté au collecteur (5) d'aspiration de mélange et disposé pour contrôler le fonctionnement du ventilateur d'évacuation (10).2. Device according to claim 1, characterized in that it further comprises a pressometric sensor (12) connected to the manifold (5) of mixture suction and arranged to control the operation of the exhaust fan (10). 3. Dispositif suivant la revendication 1, caractérisé en ce qu'un deuxième analyseur en continu (19) est connecté au collecteur de refoulement (4) à l'effet de permettre un contrôle du fonctionnement régulier du dispositif.3. Device according to claim 1, characterized in that a second continuous analyzer (19) is connected to the discharge collector (4) in order to allow a control of the regular operation of the device. 4. Dispositif suivant la revendication 1, caractérisé en ce qu'un échangeur de chaleur (22) est disposé pour opérer entre la conduite (21) d'acheminement à l'évacuation et la conduite (20) d'aspiration d'air pur, dans le but de préréchauffer l'air pur aspiré aux dépenses de la chaleur du mélange acheminé à l'évacuation.4. Device according to claim 1, characterized in that a heat exchanger (22) is arranged to operate between the pipe (21) for routing to the evacuation and the pipe (20) for suction of pure air , for the purpose of preheating the pure air drawn in at the expense of the heat of the mixture supplied to the discharge. 5. Dispositif suivant la revendication 1, auquel est connecté un dispositif (23) de dépuration du mélange acheminé à l'évacuation, caractérisé en ce qu'il comprend une connexion (25) entre la sortie dudit dispositif (23) de dépuration et l'entrée (26) pour l'air pur aspiré, en réalisant ainsi un circuit d'air partiellement fermé.5. Device according to claim 1, to which is connected a device (23) for purifying the mixture conveyed to the evacuation, characterized in that it comprises a connection (25) between the outlet of said device (23) for purifying and l inlet (26) for the aspirated clean air, thereby providing a partially closed air circuit. 6. Dispositif suivant la revendication 1, caractérisé en ce qu'il est appliqué au contrôle de la distribution de l'air à toutes les sections d'une ou plusieurs machines pour l'impression en rotogravure.6. Device according to claim 1, characterized in that it is applied to control the distribution of air to all sections of one or more machines for printing in rotogravure. 7. Dispositif suivant la revendication 1, caractérisé en ce qu'il est connecté à une pluralité de sections d'appareillages, ayant des exigences compatibles entr'elles mais non compatibles avec les exigences d'autres sections d'appareillages, ces dernières sections étant à leur tour connectées à un autre dispositif similaire.7. Device according to claim 1, characterized in that it is connected to a plurality of sections of apparatus, having requirements compatible with each other but not compatible with the requirements of other sections of apparatus, these latter sections being in turn connected to another similar device. 8. Dispositif suivant la revendication 1, caractérisé en ce qu'il comprend des soupapes d'isolement destinées (2,3) à permettre d'isoler chaque appareillage desservi, par rapport aux collecteurs (4) de refoulement et (5) d'aspiration de mélange du dispositif, pendant les périodes d'inactivité de l'appareillage considéré.8. Device according to claim 1, characterized in that it comprises isolation valves intended (2,3) to allow to isolate each apparatus served, relative to the collectors (4) of discharge and (5) of aspiration of mixing of the device, during the periods of inactivity of the apparatus considered. 9. Dispositif suivant la revendication 1, caractérisé en ce que lesdites soupapes (15,16,17) du système (14) de soupapes sont connectées entr'elles, et que le dispositif d'entraînement (18) qui les commande est unique.9. Device according to claim 1, characterized in that said valves (15,16,17) of the system (14) of valves are connected to each other, and that the drive device (18) which controls them is unique. 10. Dispositif suivant la revendication 1, caractérisé en ce qu'il comprend un ordinateur (27) lequel reçoit le signal produit par ledit analyseur (13) et pourvoit au contrôle dudit dispositif (18) d'entraînement des soupapes.10. Device according to claim 1, characterized in that it comprises a computer (27) which receives the signal produced by said analyzer (13) and provides for the control of said device (18) for driving the valves.
EP91202625A 1990-10-19 1991-10-09 Central device for distribution, recirculation and evacuation of air Withdrawn EP0481554A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT67802A IT1241275B (en) 1990-10-19 1990-10-19 CENTRALIZED DEVICE FOR DISTRIBUTION, RECIRCULATION AND AIR EVACUATION.
IT6780290 1990-10-19

Publications (1)

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EP0481554A1 true EP0481554A1 (en) 1992-04-22

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EP91202625A Withdrawn EP0481554A1 (en) 1990-10-19 1991-10-09 Central device for distribution, recirculation and evacuation of air

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EP (1) EP0481554A1 (en)
IT (1) IT1241275B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19505971A1 (en) * 1995-02-21 1996-08-22 Windmoeller & Hoelscher Drying of printed or coated rolls
DE19755812A1 (en) * 1997-12-16 1999-06-17 Zaffignani Angelo Air load regulation device in printing machine arrangement

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2022801A (en) * 1978-06-01 1979-12-19 Bebst Sa An Energy Recovery System for Use on a Printing Press or the Like
FR2465175A1 (en) * 1979-09-13 1981-03-20 Stumm Eric Nozzle drier for coated or printed web - supplies heated fresh air to final drying section connected to preliminary ones
US4343096A (en) * 1980-11-25 1982-08-10 Bobst Champlain, Inc. System for controlling emissions of a solvent from a printing press
EP0065783A1 (en) * 1981-05-25 1982-12-01 Windmöller &amp; Hölscher Device for drying printed webs in a printing machine

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2022801A (en) * 1978-06-01 1979-12-19 Bebst Sa An Energy Recovery System for Use on a Printing Press or the Like
FR2465175A1 (en) * 1979-09-13 1981-03-20 Stumm Eric Nozzle drier for coated or printed web - supplies heated fresh air to final drying section connected to preliminary ones
US4343096A (en) * 1980-11-25 1982-08-10 Bobst Champlain, Inc. System for controlling emissions of a solvent from a printing press
EP0065783A1 (en) * 1981-05-25 1982-12-01 Windmöller &amp; Hölscher Device for drying printed webs in a printing machine

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19505971A1 (en) * 1995-02-21 1996-08-22 Windmoeller & Hoelscher Drying of printed or coated rolls
ES2133035A1 (en) * 1995-02-21 1999-08-16 Windmoeller & Hoelscher Drying of printed or coated rolls
DE19505971C2 (en) * 1995-02-21 2000-08-31 Windmoeller & Hoelscher Device for drying printed or coated webs
DE19505971C5 (en) * 1995-02-21 2013-03-14 Windmöller & Hölscher Kg Apparatus for drying printed or coated webs
DE19755812A1 (en) * 1997-12-16 1999-06-17 Zaffignani Angelo Air load regulation device in printing machine arrangement
DE19755812B4 (en) * 1997-12-16 2009-01-02 Giko Verpackungen Gmbh Method and device for regulating the air charge

Also Published As

Publication number Publication date
IT1241275B (en) 1993-12-29
IT9067802A1 (en) 1992-04-19
IT9067802A0 (en) 1990-10-19

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