EP0099818B1 - Method of confining the pollution of an area by making use of an air curtain - Google Patents
Method of confining the pollution of an area by making use of an air curtain Download PDFInfo
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- EP0099818B1 EP0099818B1 EP83401438A EP83401438A EP0099818B1 EP 0099818 B1 EP0099818 B1 EP 0099818B1 EP 83401438 A EP83401438 A EP 83401438A EP 83401438 A EP83401438 A EP 83401438A EP 0099818 B1 EP0099818 B1 EP 0099818B1
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- European Patent Office
- Prior art keywords
- air
- zone
- curtain
- gas
- room
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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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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F9/00—Use of air currents for screening, e.g. air curtains
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F9/00—Use of air currents for screening, e.g. air curtains
- F24F2009/007—Use of air currents for screening, e.g. air curtains using more than one jet or band in the air curtain
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S55/00—Gas separation
- Y10S55/29—Air curtains
Definitions
- the present invention relates to methods of confining a polluted room using a gas stream and more specifically relates to such a process which allows to have a very high ratio between the level of pollution of the room and the pollution level outside of it.
- FIG. 1 An example of application of this method is illustrated in FIG. 1 in which we see, inside a cell 1, a vertical partition 2 defining a room 4 inside which is installed a machine 6 used for cutting of nuclear fuel elements.
- the room 4 containing the machine 6 communicates with the rest of the cell through an opening 8.
- the air from the vein 12 is taken up by a suction mouth 14 and sent in a circuit comprising a cyclone 16 and a fan 18.
- a suction mouth 14 The air from the vein 12 is taken up by a suction mouth 14 and sent in a circuit comprising a cyclone 16 and a fan 18.
- the air leaving the cyclone 16 is generally rejected outside the enclosure 1: as it still contains a certain amount of radioactive dust, it is necessary to filter it using an absolute filter 19 before it release into the atmosphere.
- these filters constitute very expensive materials, their replacement is a long and delicate operation because of all the protections which are necessary due to the high activity of the dusts.
- they constitute active waste which must be conditioned before their disposal. This is why it is in our interest to reduce the frequency of replacement. For this, only part of the air leaving the cyclone 16 is discharged to the outside, the other part being recycled into the nozzle 10.
- An opening 22, formed in the wall 23 of the cell 1, allows the ventilation air entering the cell in order to replace the air extracted through the filter 19 by the fan 20.
- the gas stream 12 is composed of two parts: a first part, called the "transition zone", extends over a length 1 from the slot 7 and includes a 'potential core' or 'dart' 13, consisting solely of air injected through the nozzle 10, and which has, seen, in section, the shape of a triangle of length 1, the latter being equal to approximately 6 times the width e of the injection slot.
- the gas speed is the same at all points of the sting 13 and it is equal to the injection speed.
- the second part of the gas stream 12 is a so-called 'full zone development of the jet "15 in which the air injected by the nozzle 10 mixes, by suction, with the air present in the cell 4 and in the clean zone 5 of the enclosure 1.
- the zone of full development of the jet s 'extends beyond the point of the dart, from this point to the return mouth 14.
- the zone 15 having a very turbulent regime, it sucks a large pa rtie of dust contained in cell 4 (arrows 9).
- the concentration of the pollution in the zone 5 may be of the order of half of what it is in zone 4 whereas, in the nuclear industry in particular, a concentration ratio is desired that is as low as possible and generally less than 1/100.
- the dust activates the fixed installations located in zone 5 of cell 1 and the cumulative contamination thus produced can be very significant after a certain time.
- Document DE-A-3 004 073 describes a process for ventilating premises consisting in blowing a secondary air jet through an ejector disposed in the immediate vicinity of the primary air outlet: this has the effect of increasing the range of the primary jet which would otherwise be too low because the injection speed is relatively reduced.
- This process can also be used to create an air curtain in front of a door or an opening, but, in the case of a polluted room, the dust may still escape outside for the reasons indicated more high.
- the purpose of the present invention is to remedy these drawbacks by means of a method of confining the pollution of a room communicating with the outside by means of at least one opening of the type in which a first gas stream is circulated at the level of the opening, the dimensions of this first gas stream being such that it covers the entire surface of the opening, as well as a second gas stream adjacent to the first and located on the side opposite the room relative to the latter, there first gas stream consisting of a transition zone and a zone of full development of the jet, the transition zone comprising a dart.
- it is given a length equal to the range of the first vein and the flow rates of the two gas streams are adjusted so that the air flow induced by the face of the second vein which is in contact with the first being substantially equal to the injection rate of the first vein.
- the dart covering the entire surface of the opening 8 there is no longer any risk of seeing the dust pass outside the premises through the turbulent mixing zone.
- the second gas stream its role is to stabilize the first. Indeed, for the dart to have a sufficient length, it is necessary that the width of the injection slot is equal to approximately 1 / 6th of the distance between the nozzle 10 and the suction mouth 14: this requires a low speed injection (because otherwise the flow would be prohibitive) which risks making the jet unstable.
- the second gas stream creates a suction effect which presses the first vein against the second and stabilizes it.
- the injection rate of the first vein is equal to the air flow which would have been drawn into the room if the second vein had been left alone: this prevents the first vein from being deformed by bending towards the wall lower part of room 4.
- the second vein therefore sucks, in room 4, the injection air of the first vein mixed by turbulent diffusion with a small fraction of the polluted air of room 4. It also sucks the clean air being in the zone 5 of the cell 1: therefore, the air evacuated by the suction mouth 14 is very little polluted compared to the atmosphere of the room 4.
- the air from the two gas streams is partially recycled after having taken it up through a suction mouth and passed over a purification device which can, for example, be a cyclone or a trickle tower.
- a purification device which can, for example, be a cyclone or a trickle tower.
- the energy necessary for the circulation of air is supplied by a circulation device which can be a fan, a compressor, an air ejector, etc.
- the invention also relates to an application of this process to the confinement of a room containing radioactive dust created by the cutting of nuclear fuel elements.
- the first gas stream 12 itself comprises a turbulent mixing zone 15 which sucks the air from the room 4 and therefore certain dusts contained in it (arrows 11). Part of this dust is therefore extracted through the mouth 14 while the other part is recycled into the room 4 by the induced current.
- the air sucked in through the mouth 14 is much less polluted than with the methods of the prior art. It then suffices to pass the air sucked in through this mouth 14 over a cyclone to reduce its concentration and obtain in the part 5 of the cell a concentration of polluting dust significantly lower than that of the room 4.
- FIG. 3 illustrates the application of the method according to the invention to the cell of FIG. 1.
- cell 1 fitted with the partition 2 defining room 4 containing the machine 6.
- This room is separated from the upper part 5 of the cell by a double curtain of air consisting of the first gas stream 12 leaving the nozzle 10 and the second stream 24 leaving the nozzle 25.
- the air sucked in by the return outlet 14 is first sent to cyclone 16 which decreases its concentration of pollutants.
- part of the air leaving cyclone 16 is evacuated to 1, outside of cell 1 by means of the fan 20 after passing over an absolute filter 19.
- Another part is recycled thanks to the fan 18.
- Part of this recycled air is sent to the nozzle 10 via a valve 32 and another part to the nozzle 25 via a valve 30.
- the external fan 20 and the fan 18 provide a total flow of 44,350 m 3 / h in the return outlet 14 and the cyclone 16. This flow comes on the one hand from the two gas streams 12 and 24 for 25,350 m 3 / h and on the other hand fresh air entering through opening 22 for 19,000 m 3 / h.
- the ratio of the concentrations of radioactive dust between room 4 and zone 5 of the cell is approximately 100, that is to say a value considerably higher than that which could be obtained with the processes. prior art.
- the method according to the invention has particularly advantageous advantages since it makes it possible to considerably reduce the cumulative contamination outside the room 4.
- the dust concentration of the air passing through the cyclone 16 and the absolute filter 19 is lowered, which reduces the operating cost of the installation by increasing the life of the filters 19.
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Description
La présente invention se rapporte aux procédés de confinement d'un local pollué à l'aide d'une veine gazeuse et a plus spécialement pour objet un tel procédé qui permette d'avoir un rapport très élevé entre le niveau de pollution du local et le niveau de pollution à l'extérieur de celui-ci.The present invention relates to methods of confining a polluted room using a gas stream and more specifically relates to such a process which allows to have a very high ratio between the level of pollution of the room and the pollution level outside of it.
Il est connu, notamment dans les installations nucléaires, d'isoler un local contenant une machine dégageant des poussieres radioactives en grande quantité à l'aide d'un rideau d'air afin de pouvoir intervenir facilement sur ladite machine à travers ce rideau d'air. Un exemple de mise en application de ce procédé est illustré à la figure 1 sur laquelle on voit, à l'intérieur d'une cellule 1, une cloison verticale 2 définissant un local 4 à l'intérieur duquel est installée une machine 6 servant au découpage d'éléments combustibles nucléaires. Le local 4 contenant la machine 6 communique avec le reste de la cellule par une ouverture 8. Une veine gazeuse divergente 12, sortant par une buse 10, recouvre toute la surface de l'ouverture 8 empêchant ainsi l'air pollué du local 4 de pénétrer dans la zone propre 5 de la cellule 1. L'air de la veine 12 est repris par une bouche d'aspiration 14 et envoyé dans un circuit comprenant un cyclone 16 et un ventilateur 18. Dans la suite du présent texte, on appellera 'portée du jet", ou de la veine 12, la distance parcourue par celle-ci depuis la fente d'injection 7 jusqu'à la bouche de reprise ou d'aspiration 14, et qui correspond à la largeur de l'ouverture 8.It is known, in particular in nuclear installations, to isolate a room containing a machine releasing radioactive dust in large quantities using an air curtain in order to be able to easily intervene on said machine through this curtain. air. An example of application of this method is illustrated in FIG. 1 in which we see, inside a cell 1, a vertical partition 2 defining a
L'air sortant du cyclone 16 est généralement rejeté à l'extérieur de l'enceinte 1: comme il contient encore une certaine quantité de poussieres radioactives, il est nécessaire de le filtrer à l'aide d'un filtre absolu 19 avant de le rejeter dans l'atmosphère. Cependant, outre le fait que ces filtres constituent des matériels très coûteux, leur remplacement est une opération longue et délicate à cause de toutes les protections qui sont nécessaires en raison de la forte activité des poussieres. De plus, ils constituent des déchets actifs qu'il faut conditionner avant leur évacuation. C'est pourquoi on a tout intéret à en diminuer la fréquence de remplacement. Pour cela, on ne rejette à l'extérieur qu'une partie de l'air sortant du cyclone 16, l'autre partie étant recyclée dans la buse 10. Une ouverture 22, pratiquée dans la paroi 23 de la cellule 1, permet à l'air de ventilation de pénétrer dans la cellule afin de remplacer l'air extrait à travers le filtre 19 par le ventilateur 20.The air leaving the
Un tel procédé présente des inconvénients importants. En effet, comme on peut le voir sur la figure 1, la veine gazeuse 12 se composé de deux parties: une première partie, dite 'zone de transition", s'étend sur une longueur 1 à partir de la fente 7 et comprend un 'noyau potentiel" ou 'dard" 13, constitué uniquement par de l'air injecté à travers la buse 10, et qui a sensiblement, vu en coupe, la forme d'un triangle de longueur 1, cette derniere étant égale à environ 6 fois la largeur e de la fente d'injection. La vitesse du gaz est la même en tout point du dard 13 et elle est égale à la vitesse d'injection. La deuxieme partie de la veine gazeuse 12 est une zone dite 'de plein développement du jet" 15 dans laquelle l'air injecté par la buse 10 se mélange, par aspiration, à l'air présent dans la cellule 4 et dans la zone propre 5 de l'enceinte 1. La zone de plein développement du jet s'étend au-delà de la pointe du dard, depuis cette pointe jusqu'à la bouche de reprise 14. La zone 15 ayant un régime très turbulent, elle aspire une grande partie des poussieres contenues dans la cellule 4 (fleches 9). Au-delà d'une certaine concentration dans la veine 12, ces poussieres risquent d'être rejetées dans la partie propre 5 de - l'enceinte par diffusion turbulente: dans le cas le plus défavorable, la concentration de la pollution dans la zone 5 peut être de l'ordre de la moitié de ce qu'elle est dans la zone 4 alors que, dans l'industrie nucléaire notamment, on souhaite un rapport de concentrations aussi faible que possible et généralement inférieur à 1/100. De plus, les poussieres activent les installations fixes se trouvant dans la zone 5 de la cellule 1 et la contamination cumulative ainsi produite peut être très importante au bout d'un certain temps.Such a method has significant drawbacks. In fact, as can be seen in FIG. 1, the
Afin de remédier à ce défaut, on a essaye d'augmenter la vitesse de l'air insufflé, mais cette méthode n'améliore rien et ne fait qu'augmenter les coûts d'exploitation.In order to remedy this defect, an attempt has been made to increase the speed of the supply air, but this method does not improve anything and only increases operating costs.
Une autre méthode consiste à faire circuler deux veines gazeuses au niveau de l'ouverture séparant le local de l'extérieur. Le document DE-A-3 004 073 décrit un procédé pour la ventilation de locaux consistant à insuffler un jet d'air secondaire à travers un éjecteur disposé à proximité immédiate de la sortie d'air primaire: ceci a pour effet d'augmenter la portée du jet primaire qui, sinon, serait trop faible car la vitesse d'injection est relativement réduite. Ce procédé peut aussi être utilisé pour créer un rideau d'air devant une porte ou une ouverture mais, s'il s'agit d'un local pollilé, les poussières risquent encore de s'echapper à l'extérieur pour les raisons indiquées plus haut.Another method is to circulate two gas streams at the opening separating the room from the outside. Document DE-A-3 004 073 describes a process for ventilating premises consisting in blowing a secondary air jet through an ejector disposed in the immediate vicinity of the primary air outlet: this has the effect of increasing the range of the primary jet which would otherwise be too low because the injection speed is relatively reduced. This process can also be used to create an air curtain in front of a door or an opening, but, in the case of a polluted room, the dust may still escape outside for the reasons indicated more high.
La présente invention a justement pour but de remédier à ces inconvénients grâce à un procédé de confinement de la pollution d'un local communiquant avec l'extérieur grâce à au moins une ouverture du type dans lequel on fait circuler une première veine gazeuse au niveau de l'ouverture, les dimensions de cette première veine gazeuse étant telles que celleci couvre toute la surface de l'ouverture, ainsi qu' une deuxième veine gazeuse adjacente à la première et située du côté opposé au local par rapport à celle-ci-, là première veine gazeuse se composant d'une zone de transition et d'une zone de plein développement du jet, la zone de transition comportant un dard. Selon l'invention, on donne à celui-ci une longueur égale à la portée de la première veine et on règle les débits des deux veines gazeuses de sorte que le débit d'air induit par la face de la deuxieme veine qui est en contact avec la première soit sensiblement egal au débit d'injection de la première veine.The purpose of the present invention is to remedy these drawbacks by means of a method of confining the pollution of a room communicating with the outside by means of at least one opening of the type in which a first gas stream is circulated at the level of the opening, the dimensions of this first gas stream being such that it covers the entire surface of the opening, as well as a second gas stream adjacent to the first and located on the side opposite the room relative to the latter, there first gas stream consisting of a transition zone and a zone of full development of the jet, the transition zone comprising a dart. According to the invention, it is given a length equal to the range of the first vein and the flow rates of the two gas streams are adjusted so that the air flow induced by the face of the second vein which is in contact with the first being substantially equal to the injection rate of the first vein.
Ainsi, le dard couvrant toute la surface de l'ouverture 8 on ne risque plus de voir les poussieres passer à l'extérieur du local à travers la zone de mélange turbulent. Quant à la deuxieme veine gazeuse, elle a pour rôle de stabiliser la première. En effet, pour que le dard ait une longueur suffisante, il faut que la largeur de la fente d'injection soit égale à 1/6e environ de la distance entre la buse 10 et la bouche d'aspiration 14: ceci impose une faible vitesse d'injection (car sinon le débit serait prohibitif) qui risque de rendre le jet instable. La deuxième veine gazeuse crée un effet d'aspiration qui plaque la première veine contre la deuxième et la stabilise.Thus, the dart covering the entire surface of the opening 8 there is no longer any risk of seeing the dust pass outside the premises through the turbulent mixing zone. As for the second gas stream, its role is to stabilize the first. Indeed, for the dart to have a sufficient length, it is necessary that the width of the injection slot is equal to approximately 1 / 6th of the distance between the
D'autre part, le debit d injection de la première veine est égal au débit d'air qui aurait été aspiré dans le local si on avait laissé la deuxième veine seule: on évite ainsi que la première veine se déforme par infléchissement vers la paroi inférieure du local 4. La deuxième veine aspire donc, dans le local 4, l'air d'injection de la première veine mélangé par diffusion turbulente à une faible fraction de l'air pollué du local 4. Elle aspire d'autre part de l'air propre se trouvant dans la zone 5 de la cellule 1: de ce fait, l'air évacué par la bouche d'aspiration 14 est très peu pollué par rapport à l'atmosphère du local 4.On the other hand, the injection rate of the first vein is equal to the air flow which would have been drawn into the room if the second vein had been left alone: this prevents the first vein from being deformed by bending towards the wall lower part of
Selon une autre caractéristique du procédé objet de l'invention, on recycle partiellement l'air des deux veines gazeuses après l'avoir repris par une bouche d'aspiration et fait passer sur un appareil d'épuration qui peut être, par exemple, un cyclone ou une tour a ruissellement. L'énergie nécessaire à la mise en circulation de l'air est fournie par un appareil de circulation qui peut être un ventilateur, un compresseur, un éjecteur d'air, etc...According to another characteristic of the process which is the subject of the invention, the air from the two gas streams is partially recycled after having taken it up through a suction mouth and passed over a purification device which can, for example, be a cyclone or a trickle tower. The energy necessary for the circulation of air is supplied by a circulation device which can be a fan, a compressor, an air ejector, etc.
Enfin, l'invention a également pour objet une application de ce procédé au conf inement d'un local contenant des poussières radioactives créées par le découpage d'éléments combustibles nucléaires.Finally, the invention also relates to an application of this process to the confinement of a room containing radioactive dust created by the cutting of nuclear fuel elements.
L'invention apparaitra mieux à la lecture de la description qui va suivre, donnée à titre d'exemple purement illustratif et nullement limitatif, en réference aux dessins annexés, dans lesquels:
- - la figure 1, déjà décrite, est une vue schématique en coupe illustrant um procédé de confinement d'un local selon l'art antérieur;
- - la figure 2 est une vue schématique en coupe montrant les deux veines gazeuses utilisées dans le procédé objet de l'invention, et
- - la figure 3 est une vue schématique en coupe semblable à la figure 1 montrant l'application du procédé selon l'invention au même local:
- Sur la figure 2, on voit qu'on a transformé la
buse 10 en donnant à la fente d'injection 7 une largeur suffisante pour que l'extrémité dudard 13 de la première veine se trouve au niveau de la bouche dereprise 14. Selon l'invention, on pilote cettepremiere veine 12 à l'aide d'une deuxième veine gazeuse 24 qui arrive par unebuse 25 placée au voisinage immédiat de labuse 10. Les débits sont calculés pour que laveine 24 aspire, du côte dulocal 4, un débit d'air égal au débit d'injection de la première veine: comme ledard 13 couvre toute la surface de l'ouverture 8, et empêche ainsi les poussières de passer à l'extérieur dulocal 4, c'est de l'air peu pollué qui est aspiré par labouche 14.
- Sur la figure 2, on voit qu'on a transformé la
- - Figure 1, already described, is a schematic sectional view illustrating a method of confining a room according to the prior art;
- FIG. 2 is a schematic sectional view showing the two gas streams used in the process which is the subject of the invention, and
- FIG. 3 is a schematic sectional view similar to FIG. 1 showing the application of the method according to the invention to the same room:
- In FIG. 2, it can be seen that the
nozzle 10 has been transformed by giving the injection slot 7 a width sufficient for the end of thedart 13 of the first vein to be at the level of thereturn mouth 14. According to the invention, thisfirst stream 12 is piloted using asecond gas stream 24 which arrives by anozzle 25 placed in the immediate vicinity of thenozzle 10. The flow rates are calculated so that thestream 24 sucks, from the side fromroom 4, an air flow equal to the injection flow from the first vein: as thesting 13 covers the entire surface of theopening 8, and thus prevents dust from passing outside ofroom 4, c is little polluted air which is sucked in through themouth 14.
- In FIG. 2, it can be seen that the
En réalité, une petite partie des poussières contenues dans le local 4 est évacuée par la bouche 14 pour la raison suivante: en effet, la première veine gazeuse 12 comporte elle-même une zone de mélange turbulent 15 qui aspire l'air du local 4 et donc certaines poussières contenues dans celle-ci (flèches 11 ). Une partie de ces poussières est donc extraite par la bouche 14 tandis que l'autre partie est recyclée dans le local 4 par le courant induit. Cependant, l'air aspiré par la bouche 14 est beaucoup moins pollué qu'avec les procédés de l'art antérieur. Il suffit alors de faire passer l'air aspiré par cette bouche 14 sur un cyclone pour diminuer sa concentration et obtenir dans la partie 5 de la cellule une concentration en poussieres polluantes notablement inférieure à celle du local 4.In reality, a small part of the dust contained in the
La figure 3 illustre l'application du procédé selon l'invention à la cellule de la figure 1. Sur cette figure, on voit encore la cellule 1 équipée de la cloison 2 déf inissant le local 4 contenant la machine 6. Ce local est séparé de la partie supérieure 5 de la cellule par un double rideau d'air constitué de la première veine gazeuse 12 sortant de la buse 10 et de la deuxième veine 24 sortant de la buse 25. L'air aspiré par la bouche de reprise 14 est d'abord envoyé sur le cyclone 16 qui diminue sa concentration en polluants. Comme dans l'exemple de la figure 1, une partie de l'air sortant du cyclone 16 est évacuée à 1,ex-térieur de la cellule 1 grâce au ventilateur 20 après être passée sur un filtre absolu 19. Une autre partie est recyclée grâce au ventilateur 18. Une partie de cet air recyclé est envoyée dans la buse 10 par l'intermédiaire d'une vanne 32 et une autre partie dans la buse 25 par l'intermédiaire d'une vanne 30.FIG. 3 illustrates the application of the method according to the invention to the cell of FIG. 1. In this figure, we can still see cell 1 fitted with the partition 2 defining
A titre d'exemple, on a appliqué le procédé objet de l'invention à une cellule telle que 1, contenant une machine 6 servant au découpage d'éléments combustibles nucléaires. L'ouverture 8 séparant le local 4 de la zone supérieure 5 de la cellule a une longueur de 9 m pour une largeur de 3 m. La distance entre la sortie de la buse 10 et l'entrée de la bouche d'aspiration 14 est de 2,4 m. Le débit total d'air entrant dans la cellule est de 44 350 m3/h dont 19 000 m3/h d'air frais entrant dans la cellule par l'ouverture 22 et 25 350 m3/h d'air recyclé. Celui-ci est partagé de la manière suivante:
- - 6 350 m3/h passent à travers la
buse 25 pour créer la deuxième veine rapide 24; et - -19 000 m3/h passent à travers la
buse 10 pour créer la première veine lente 12.
- - 6,350 m 3 / h pass through the
nozzle 25 to create the secondrapid vein 24; and - -19,000 m 3 / h pass through the
nozzle 10 to create the firstslow vein 12.
Le ventilateur extérieur 20 et le ventilateur 18 assurent un débit total de 44 350 m3/h dans la bouche de reprise 14 et le cyclone 16. Ce débit provient d'une part des deux veines gazeuses 12 et 24 pour 25 350 m3/h et d'autre part de l'air frais entrant par l'ouverture 22 pour 19 000 m3/h. Avec les valeurs de débit indiquées ci-dessus, le rapport des concentrations en poussières radioactives entre le local 4 et la zone 5 de la cellule est d'environ 100, soit une valeur notablement supérieure à celles que l'on pouvait obtenir avec les procédés de l'art anterieur.The
De plus, d'autres séries d'essais ont montré qu'il etait possible de faire passer un bras de télémanipulateur à travers un rideau d'air conforme à l'invention sans perturber de façon sensible l'efficacité du confinement.In addition, other series of tests have shown that it was possible to pass a manipulator arm through an air curtain according to the invention without appreciably disturbing the effectiveness of the confinement.
Le procédé selon l'invention présente des avantages particulièrement intéressants puisqu'il permet de diminuer considérablement la contamination cumulative à l'extérieur du local 4. De plus, la concentration en poussières de l'air passant à travers le cyclone 16 et le filtre absolu 19 est abaissée, ce qui diminue le coût d'exploitation de l'installation en augmentant la durée de vie des filtres 19.The method according to the invention has particularly advantageous advantages since it makes it possible to considerably reduce the cumulative contamination outside the
Quant aux applications du procédé, elles sont nombreuses et variées et ne se limitent pas è l'industrie nucléaire. On peut, par exemple dans l'industrie chimique, isoler de la même manière un local où sont manipulés des produits particulièrement toxiques. Par exemple, dans le cas d'installations produisant du chlore, on peut utiliser une tour à ruissellement de solutions alcalines à la placé du cyclone et du filtre pour éliminer le chlore. Enfin, le procédé s'applique à toute installation produisant des poussières en grande quantité, que celles-ci soient radioactives ou non.As for the applications of the process, they are numerous and varied and are not limited to the nuclear industry. One can, for example in the chemical industry, isolate in the same way a room where are handled particularly toxic products. For example, in the case of installations producing chlorine, an alkaline solution trickle tower can be used in place of the cyclone and the filter to remove the chlorine. Finally, the process applies to any installation producing large quantities of dust, whether or not it is radioactive.
Claims (5)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8212382 | 1982-07-15 | ||
FR8212382A FR2530163B1 (en) | 1982-07-15 | 1982-07-15 | METHOD FOR CONTAINING THE POLLUTION OF A PREMISES USING A GAS VEIN |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0099818A1 EP0099818A1 (en) | 1984-02-01 |
EP0099818B1 true EP0099818B1 (en) | 1986-02-26 |
Family
ID=9275993
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP83401438A Expired EP0099818B1 (en) | 1982-07-15 | 1983-07-12 | Method of confining the pollution of an area by making use of an air curtain |
Country Status (5)
Country | Link |
---|---|
US (1) | US4576613A (en) |
EP (1) | EP0099818B1 (en) |
JP (1) | JPS5924297A (en) |
DE (1) | DE3362295D1 (en) |
FR (1) | FR2530163B1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4234250A1 (en) * | 1992-10-10 | 1994-04-14 | Hartwig Sylvius Univ Prof Dr | Air curtain system for confining accidental gas discharge - having segmented nozzle pipe individually operating with air or inert gas |
Families Citing this family (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2621887B1 (en) * | 1987-10-20 | 1990-03-30 | Sgn Soc Gen Tech Nouvelle | DYNAMIC CONTAINMENT AND NON-CONTACT MOUNTING |
GB2220255B (en) * | 1988-05-13 | 1992-01-02 | Heinz Hoelter | A method of,and apparatus for cooling and keeping clean the roof of a coke oven |
DE3836278A1 (en) * | 1988-10-25 | 1990-04-26 | Schlick Heinrich Gmbh Co Kg | Device for blasting, or the like, the inner surfaces of channels with granular material |
US4902313A (en) * | 1989-04-17 | 1990-02-20 | Penter Albert P | Apparatus and method of reducing pollution for tire buffing equipment |
FR2652520B1 (en) * | 1989-10-02 | 1992-02-07 | Sgn Soc Gen Tech Nouvelle | METHOD AND DEVICE FOR MAINTAINING A CLEAN ATMOSPHERE WITH REGULATED TEMPERATURE ON A WORKSTATION. |
FR2659782B1 (en) * | 1990-03-14 | 1992-06-12 | Sgn Soc Gen Tech Nouvelle | METHOD AND DEVICE FOR DYNAMIC SEPARATION OF TWO ZONES. |
FR2662296B1 (en) * | 1990-05-15 | 1994-06-17 | Cogema | REMOTE SANITATION INSTALLATION, BY DEGRADATION, OF A SURFACE LOCATED IN HOSTILE ENVIRONMENT, WITH RECOVERY AND TREATMENT OF WASTE. |
US5338248A (en) * | 1993-01-25 | 1994-08-16 | Midwest Air Products Co., Inc. | Ventilation apparatus for removing vapors |
US5457270A (en) * | 1993-10-04 | 1995-10-10 | Hildebrand; Philip B. | Chemical control system for confining volatile liquids |
FR2730297B1 (en) * | 1995-02-02 | 1997-05-09 | Soc Generale Pour Les Techniques Nouvelles Sgn | CONTAINMENT METHOD AND DEVICE, ESPECIALLY OF A PARTICULAR ATMOSPHERE IN A CONTINUOUS PROCESSING SPACE OF THROUGHPUT PRODUCTS |
US5711705A (en) * | 1995-05-25 | 1998-01-27 | Flanders Filters, Inc. | Isolation work station |
FR2740205B1 (en) * | 1995-10-23 | 1998-01-09 | Unir Ultra Propre Nutrition In | PROTECTION AGAINST AEROCONTAMINATION |
FR2756910B1 (en) | 1996-12-10 | 1999-01-08 | Commissariat Energie Atomique | PROCESS FOR DYNAMIC SEPARATION OF TWO AREAS BY A CLEAN AIR CURTAIN |
FR2757933B1 (en) | 1996-12-27 | 1999-01-22 | Commissariat Energie Atomique | DEVICE FOR DYNAMICALLY SEPARATING TWO ZONES BY AT LEAST ONE BUFFER ZONE AND TWO CURTAINS OF CLEAN AIR |
FR2760199B1 (en) | 1997-03-03 | 1999-05-21 | Unir Ultra Propre Nutrition In | DEVICE FOR SEPARATING TWO ZONES WITH DIFFERENT ATMOSPHERES |
FR2770330B1 (en) | 1997-10-24 | 2000-01-14 | Cogema | METHOD AND DEVICE FOR CONTAINMENT BY THERMAL LAMINATION |
US6503324B1 (en) | 2000-07-27 | 2003-01-07 | Howmet Research Corporation | Stucco tower and method |
NL1027520C2 (en) * | 2004-11-16 | 2006-05-17 | Haskoning Nederland B V | Climate control system for painting on display, comprises flow of air parallel to wall and forming barrier between painting and surrounding atmosphere |
FR2928718B1 (en) * | 2008-03-11 | 2010-12-10 | Bhd Ingenierie | GAS EMISSION EVACUATION SYSTEM PROVIDED BY AT LEAST ONE EMISSIVE POSITION IN A LOCAL |
FR2990143B1 (en) * | 2012-05-07 | 2015-01-30 | Paul Brunon | MULTI-JET BLOWING NOZZLE |
CN103264033B (en) * | 2013-05-21 | 2015-09-30 | 山东泰北环保设备股份有限公司 | A kind of workshop toxic and harmful treatment facility |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2593702A (en) * | 1948-04-13 | 1952-04-22 | Claude B Schneible | Gaseous curtain for ventilating exhaust |
GB1237694A (en) * | 1968-08-19 | 1971-06-30 | Progress Jets Ltd | Improvements relating to air curtains |
DE2002349C3 (en) * | 1970-01-20 | 1975-11-27 | Brueckner-Apparatebau Gmbh, 6122 Erbach | Device for the sealing implementation of a web-shaped material through a slot |
SE350114B (en) * | 1970-07-01 | 1972-10-16 | Svenska Flaektfabriken Ab | |
JPS50146961A (en) * | 1974-05-16 | 1975-11-25 | ||
DE3004073A1 (en) * | 1980-02-05 | 1981-08-13 | TTL Tür + Torschleier lufttechnische Geräte GmbH, 7065 Winterbach | Ventilation equipment for room - has high-pressure fan supplying room air to secondary air ejector nozzles |
-
1982
- 1982-07-15 FR FR8212382A patent/FR2530163B1/en not_active Expired
-
1983
- 1983-07-11 US US06/512,619 patent/US4576613A/en not_active Expired - Lifetime
- 1983-07-12 EP EP83401438A patent/EP0099818B1/en not_active Expired
- 1983-07-12 DE DE8383401438T patent/DE3362295D1/en not_active Expired
- 1983-07-14 JP JP58127019A patent/JPS5924297A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4234250A1 (en) * | 1992-10-10 | 1994-04-14 | Hartwig Sylvius Univ Prof Dr | Air curtain system for confining accidental gas discharge - having segmented nozzle pipe individually operating with air or inert gas |
Also Published As
Publication number | Publication date |
---|---|
FR2530163B1 (en) | 1986-08-29 |
JPS5924297A (en) | 1984-02-07 |
US4576613A (en) | 1986-03-18 |
JPH0519119B2 (en) | 1993-03-15 |
EP0099818A1 (en) | 1984-02-01 |
FR2530163A1 (en) | 1984-01-20 |
DE3362295D1 (en) | 1986-04-03 |
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