EP2794117B1 - Device for generating an aerosol with a controlled particle size - Google Patents
Device for generating an aerosol with a controlled particle size Download PDFInfo
- Publication number
- EP2794117B1 EP2794117B1 EP12805701.5A EP12805701A EP2794117B1 EP 2794117 B1 EP2794117 B1 EP 2794117B1 EP 12805701 A EP12805701 A EP 12805701A EP 2794117 B1 EP2794117 B1 EP 2794117B1
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- EP
- European Patent Office
- Prior art keywords
- container
- aerosol
- lower container
- channel
- base
- Prior art date
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- 239000000443 aerosol Substances 0.000 title claims description 32
- 239000002245 particle Substances 0.000 title claims description 32
- 239000000843 powder Substances 0.000 claims description 20
- 239000006185 dispersion Substances 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 6
- 238000007789 sealing Methods 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 2
- 239000000725 suspension Substances 0.000 description 8
- 235000021183 entrée Nutrition 0.000 description 4
- 229910000906 Bronze Inorganic materials 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 239000010974 bronze Substances 0.000 description 2
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002109 single walled nanotube Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/0012—Apparatus for achieving spraying before discharge from the apparatus
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/14—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas designed for spraying particulate materials
- B05B7/1404—Arrangements for supplying particulate material
- B05B7/144—Arrangements for supplying particulate material the means for supplying particulate material comprising moving mechanical means
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/14—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas designed for spraying particulate materials
- B05B7/1404—Arrangements for supplying particulate material
- B05B7/1463—Arrangements for supplying particulate material the means for supplying particulate material comprising a gas inlet for pressurising or avoiding depressurisation of a powder container
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B4/00—Separating solids from solids by subjecting their mixture to gas currents
Definitions
- the invention relates to a device and a method for generating an aerosol from a powder.
- An aerosol is a set of solid or liquid particles of a chemical substance suspended in a gaseous medium.
- a powder is mixed with bronze balls in a test tube.
- the suspension of the particles for the generation of the aerosol is carried out by shaking the tube (either by rotating or by vibration) while injecting a flow of air from the top of the test tube, the aerosol being extracted from the top of the tube as well.
- a problem with these techniques is that the reproducibility over time of the generated aerosol is not guaranteed.
- the particle size of the aerosol particles is very variable, in particular because of the presence of aggregates.
- the invention proposes a device for generating an aerosol whose particle size is controlled, in particular the maximum size of the particles extracted.
- the arrangement of the pipe makes it possible to inject air directly into the production zone, at the point where the particles are suspended.
- the rising airflow in the selection zone allows sorting of the particle sizes by vertical elutriation.
- the upper container is conical in shape which provides a stable upward flow without turbulence at the connection with the dispersion zone.
- the lower container is removable, allowing easy cleaning and powder filling without disassembling the entire dispersion system.
- the invention makes it possible to control the rate of suspension of the particles, independently of the flow rate of air injected.
- a device for generating a controlled particle size aerosol, from a powder P is composed of a dispersion system 1, 2 of the particles comprising a lower container 1 said zone in which a powder P to suspend is deposited and an upper container 2 said selection area.
- the production zone means the zone in which the particles are suspended and, by zone of selection, the zone in which particles originating from the powder P having a certain particle size are selected to generate a certain type of aerosol.
- the upper container 2 comprises an upper base 2a having an inlet port 2e and a lower base 2b in aeraulic connection with the lower vessel 1 and an intermediate portion 2d between the upper base 2a and the lower base 2b.
- the intermediate portion 2d includes an aerosol outlet port 2c disposed in the upper portion of the upper base 2a.
- the outlet 2c is in particular arranged on one side of the upper part of the upper container 2.
- the upper part is understood to mean an area that extends from the top of the upper container 2 to the half of the upper container 2, preferably to one third of the upper container 2.
- the inlet port 2e may be disposed on the intermediate portion 2d and the outlet port 2c may be disposed on the upper base 2a.
- the generating device comprises a channel 3 directly dipping into the lower container 1.
- the channel 3 is for example made of metal and is in particular vertical to extend along an axis of longitudinal symmetry of the upper container 2 in the case of the figure 1 otherwise the channel 3 may be arranged in another way, especially if the inlet orifice 2e is disposed on the intermediate portion 2d and the outlet orifice 2c on the upper base 2a.
- the channel 3 has an internal section which is dimensioned to obtain a turbulent air jet in the lower container 1.
- the inner section of the channel 3 may be square, ellipsoidal or preferably circular.
- the channel 3 is connected to an air supply (not shown) and the injected air is in particular clean air obtained from a conventional compressed air source, the air coming from the source of air. compressed air having been previously dried and filtered.
- the internal section of channel 3 is dimensioned according to the air flow, so as to produce a turbulent air jet directly in the lower part 1.
- a flow meter (not shown) between the 2nd inlet of the channel 3 and the air supply is used.
- the generation device also comprises an agitator 4 which is for example of the Vortex Genius 3® type.
- the stirrer 4 comprises a housing for maintaining the dispersion system via the lower container 1.
- the agitator 4 makes it possible to rotate the dispersion system.
- the channel 3 is arranged relative to the upper container 2 so that the dispersion system can have a rotational movement without being hindered by it.
- the arrival of the air flow is by means of the channel 3 which is vertical and which directly plunges into the lower container 1 and which makes it possible to transport the suspended particles, thanks to the agitation powder P caused by the stirrer 4 in the lower container 1, to the outlet 2c.
- the generating device comprises a sealing member 5 for sealing between the channel 3 and the contour of the orifice 2e.
- the channel 3 is in particular integral with the upper container 2.
- the outlet orifice 2c is disposed sufficiently far from the end of the channel 3 immersed in the lower container.
- outlet orifice 2c must be located in the part where the section of the upper container is the largest because it is this section which is used to calculate the speeds in the system and which determines the size of the selected particles ( see below).
- the upper container 2 is further dimensioned in a certain way. In Indeed, depending on the size and shape of the latter can be selected particles having a certain particle size.
- the conical shape of the upper container 2 makes it possible to obtain a stable flow during the passage of the aerosol through the upper base 2b in connection with the lower container 1.
- the diameter of the upper base 2a makes it possible to impose a specific upward flow velocity limiting the extraction of particles having an aerodynamic diameter greater than a critical value defined by the size of the upper base 2a and the air flow injected into the system through channel 3.
- the upper container 2 is such that the intermediate portion 2d is convergent between the upper base 2a and the lower base.
- the upper container 2 is conical. It is in particular the internal section of the upper container 2 which will make it possible to control the maximum particle size of the aerosol generated.
- the latter has a bottom having a hemispherical section
- Such a hemispherical section has the further advantage of being easily cleaned (no sharp angle).
- this hemispherical section is suitable for adapting the lower container 1 to the stirrer 4.
- the lower container has a section wider than the lower base of the upper container 2.
- the lower container 1 is removable relative to the upper container 2.
- the generation device has the following parameters: feed air flow rate between 0 , 1 L / min and 0.5 L / min; concentration variability less than 5% over one hour of production.
Description
L'invention concerne un dispositif et un procédé de génération d'un aérosol à partir d'une poudre.The invention relates to a device and a method for generating an aerosol from a powder.
Un aérosol est un ensemble de particules solides ou liquides d'une substance chimique en suspension dans un milieu gazeux.An aerosol is a set of solid or liquid particles of a chemical substance suspended in a gaseous medium.
On connait diverses techniques pour générer un aérosol à partir d'une poudre et on connait notamment les techniques décrites dans les documents suivants :
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Baron P., Maynard A. Foley M. : « Evaluation of aerosol release during the handling of unrefined single walled carbon nanotube material, » NIOSH DART-02-191 rev 1.1 April 2003 -
Ku B.K., Maynard A.D., Baron P.A., Deye G.J.: « Observation and measurement of anomalous responses in a differential mobility analyzer caused by ultrafine fibrous carbon aerosols, » Journal of Electrostatics, 65, 542-548 -
Maynard A., Baron P., Foley M., Shvedova A., Kisin E., Castranova V.: « Exposure to carbon nanotube material: aerosol release during the handling of unrefined single-walled carbon nanotube material, » J. Toxicol. Env. Health part A, 67, 87-107
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Baron P., Maynard A. Foley M .: "Evaluation of aerosol release during the handling of a single walled carbon nanotube material," NIOSH DART-02-191 rev 1.1 April 2003 -
Ku BK, Maynard AD, Baron PA, Deye GJ: "Observation and measurement of anomalous responses in a differential mobility analyzer caused by ultrafine fibrous carbon aerosols," Journal of Electrostatics, 65, 542-548 -
Maynard A., Baron P., Foley M., Shvedova A., Kisin E., Castranova V .: "Exposure to carbon nanotube material: aerosol release during the handling of a single-walled carbon nanotube material," J. Toxicol. Approx. Health part A, 67, 87-107
Dans ces documents, pour générer un aérosol, une poudre est mélangée avec des billes en bronze dans un tube à essais. La mise en suspension des particules pour la génération de l'aérosol est effectuée en agitant le tube (soit par mise en rotation soit par vibration) tout en injectant un débit d'air par le haut du tube à essais, l'aérosol étant extrait par le haut du tube également.In these documents, to generate an aerosol, a powder is mixed with bronze balls in a test tube. The suspension of the particles for the generation of the aerosol is carried out by shaking the tube (either by rotating or by vibration) while injecting a flow of air from the top of the test tube, the aerosol being extracted from the top of the tube as well.
On connait de plus le document
Un problème avec ces techniques est que la reproductibilité dans le temps de l'aérosol généré n'est pas garantie. En particulier, la granulométrie des particules de l'aérosol est très variable, notamment du fait de la présence d'agrégats.A problem with these techniques is that the reproducibility over time of the generated aerosol is not guaranteed. In particular, the particle size of the aerosol particles is very variable, in particular because of the presence of aggregates.
L'invention propose un dispositif de génération d'un aérosol dont la granulométrie est contrôlée, notamment la taille maximale des particules extraites.The invention proposes a device for generating an aerosol whose particle size is controlled, in particular the maximum size of the particles extracted.
A cet effet, l'invention propose un dispositif de génération d'un aérosol à granulométrie contrôlée, à partir d'une poudre, le dispositif comprenant :
- un système de dispersion des particules comprenant :
- o un récipient inférieur dit zone de production adapté pour recevoir une poudre ;
- o un récipient supérieur dit zone de sélection comprenant une base supérieure ; un orifice d'entrée ; une base inférieure en liaison aéraulique avec le récipient inférieur ; une partie intermédiaire entre la base supérieure et la base inférieure ; un orifice de sortie disposé en partie supérieure de la base supérieure ;
- un canal plongeant de l'orifice d'entrée jusque dans le récipient inférieur pour acheminer de l'air directement dans ledit récipient inférieur, la section interne du canal étant dimensionnée pour obtenir un jet d'air turbulent dans le récipient inférieur.
- le dispositif étant caractérisé en ce qu'il comprend en outre: un agitateur comprenant un logement adapté pour loger le récipient inférieur et mettre en rotation le système de dispersion ;
- a particle dispersion system comprising:
- o a lower container said production area adapted to receive a powder;
- o an upper container said selection area comprising an upper base; an inlet port; a lower base in aeraulic connection with the lower container; an intermediate portion between the upper base and the lower base; an outlet disposed in the upper portion of the upper base;
- a channel plunging from the inlet port into the lower vessel for conveying air directly into said lower vessel, the inner section of the channel being sized to provide a turbulent air jet into the lower vessel.
- the device being characterized in that it further comprises: an agitator comprising a housing adapted to house the lower container and rotating the dispersion system;
L'invention est avantageusement complétée par les caractéristiques suivantes, prises seules ou en une quelconque de leur combinaison - techniquement possible :
- le récipient supérieur présente un axe de symétrie longitudinal le long duquel s'étend le canal ;
- le récipient supérieur est dimensionné en fonction de la granulométrie souhaitée pour l'aérosol ;
- l'orifice d'entrée est sur la base supérieure et dans lequel l'orifice de sortie est sur la partie intermédiaire ;
- la partie intermédiaire est convergente entre la base supérieure et la base inférieure ;
- le récipient inférieur présente une section hémisphérique ;
- le récipient inférieur est amovible par rapport au récipient supérieur ;
- il comprend en outre un élément d'étanchéité entourant le canal pour assurer l'étanchéité entre le canal et le contour de l'orifice d'entrée.
- the upper container has a longitudinal axis of symmetry along which the channel extends;
- the upper container is sized according to the desired particle size for the aerosol;
- the inlet port is on the upper base and in which the outlet port is on the intermediate portion;
- the intermediate portion is convergent between the upper base and the lower base;
- the lower container has a hemispherical section;
- the lower container is removable relative to the upper container;
- it further comprises a sealing member surrounding the channel for sealing between the channel and the contour of the inlet port.
L'invention propose également un procédé de génération d'un aérosol au moyen d'un dispositif de génération selon l'invention, comprenant les étapes suivantes :
- disposer une poudre dans le récipient inférieur ;
- amener de l'air au moyen du canal dans le récipient inférieur pour mettre en suspension des particules issues de la poudre pour générer un aérosol ;
- mettre en agitation/rotation le système de génération au moyen de l'agitateur ;
- récupérer l'aérosol ainsi généré par l'orifice de sortie.
- dispose a powder in the lower container;
- supplying air through the channel into the lower vessel to suspend particles from the powder to generate an aerosol;
- stirring / rotating the generating system by means of the stirrer;
- recover the aerosol thus generated by the outlet orifice.
Les avantages de l'invention sont multiples.The advantages of the invention are manifold.
La présence des zones de production et de sélection se traduit par la présence de deux zones aérauliques dans le même système permettant respectivement la mise en suspension et la sélection en taille de l'aérosol.The presence of the production and selection zones results in the presence of two aeraulic zones in the same system respectively allowing the suspension and the size selection of the aerosol.
La disposition du tuyau permet d'injecter de l'air directement dans la zone de production, à l'endroit de la mise en suspension des particules.The arrangement of the pipe makes it possible to inject air directly into the production zone, at the point where the particles are suspended.
L'écoulement d'air ascendant dans la zone de sélection permet le tri des tailles de particule par élutriation verticale.The rising airflow in the selection zone allows sorting of the particle sizes by vertical elutriation.
Le récipient supérieur est de forme conique ce qui permet d'obtenir un écoulement ascendant stable sans turbulence au niveau de la connexion avec la zone de dispersion.The upper container is conical in shape which provides a stable upward flow without turbulence at the connection with the dispersion zone.
Le récipient inférieur est démontable, ce qui permet un nettoyage et un remplissage de poudre facile sans démonter l'ensemble du système de dispersion.The lower container is removable, allowing easy cleaning and powder filling without disassembling the entire dispersion system.
Avec l'invention il est possible d'utiliser de très faibles débits d'air, inférieurs par exemple à 1 L/min, ce qui permet de créer facilement un confinement de la poudre par cascade de pression.With the invention it is possible to use very low air flows, for example less than 1 L / min, which makes it easy to create a confinement of the powder by cascade of pressure.
L'invention permet une maîtrise du taux de mise en suspension des particules, indépendamment du débit d'air injecté.The invention makes it possible to control the rate of suspension of the particles, independently of the flow rate of air injected.
Enfin avec l'invention on obtient une très bonne stabilité et une très bonne reproductibilité de la concentration sur plusieurs heures de fonctionnement grâce à la combinaison de deux zones aérauliques.Finally, with the invention, a very good stability and a very good reproducibility of the concentration over several hours of operation are obtained thanks to the combination of two aeraulic zones.
D'autres caractéristiques, buts et avantages de l'invention ressortiront de la description qui suit, qui est purement illustrative et non limitative, et qui doit être lue en regard de la
Un dispositif de génération d'un aérosol à granulométrie contrôlée, à partir d'une poudre P, conforme à un mode de réalisation de l'invention est composé d'un système de dispersion 1, 2 des particules comprenant un récipient inférieur 1 dit zone de production, dans lequel une poudre P à mettre en suspension est déposée et un récipient supérieur 2 dit zone de sélection.A device for generating a controlled particle size aerosol, from a powder P, according to one embodiment of the invention is composed of a
On précise que l'on entend par zone de production, la zone dans laquelle les particules sont mises en suspension et par zone de sélection la zone dans laquelle des particules issues de la poudre P présentant une certaine granulométrie sont sélectionnées pour générer un certain type d'aérosol.It is specified that the production zone means the zone in which the particles are suspended and, by zone of selection, the zone in which particles originating from the powder P having a certain particle size are selected to generate a certain type of aerosol.
Le récipient supérieur 2 comprend une base supérieure 2a ayant un orifice d'entrée 2e et, une base inférieure 2b en liaison aéraulique avec le récipient inférieur 1 et une partie intermédiaire 2d entre la base supérieure 2a et la base inférieure 2b.The
La partie intermédiaire 2d comprend un orifice de sortie 2c d'aérosol disposée dans la partie supérieure de la base supérieure 2a. La sortie 2c est en particulier disposée sur un côté de la partie supérieure du récipient supérieur 2.The
On précise que l'on entend par partie supérieure, une zone qui s'étend du haut du récipient supérieur 2 jusqu'à la moitié du récipient supérieur 2, de préférence jusqu'au tiers du récipient supérieur 2.It is specified that the upper part is understood to mean an area that extends from the top of the
De manière alternative l'orifice d'entrée 2e peut être disposé sur la partie intermédiaire 2d et l'orifice de sortie 2c peut être disposé sur la base supérieure 2a.Alternatively the
Afin d'amener l'air directement dans le récipient inférieur 1, le dispositif de génération comprend en canal 3 plongeant directement dans le récipient inférieur 1. Le canal 3 est par exemple en métal et est notamment vertical pour s'étendre selon un axe de symétrie longitudinal du récipient supérieur 2 dans le cas de la
Le canal 3 présente une section interne qui est dimensionnée pour obtenir un jet d'air turbulent dans le récipient inférieur 1.The
La section interne du canal 3 peut être carrée, ellipsoïdale ou de préférence circulaire.The inner section of the
Le canal 3 est connecté à une alimentation d'air (non représentée) et l'air injecté est en particulier de l'air propre obtenu à partir d'une source d'air comprimée classique, l'air issu de la source d'air comprimé ayant été préalablement séché et filtré. Ainsi, la section interne du canal 3 est dimensionnée en fonction du débit d'air, de façon à produire un jet d'air turbulent directement dans la partie inférieure 1.The
En outre, pour contrôler le débit d'air injecté, un débitmètre (non représenté) entre l'orifice d'entrée 2e du canal 3 et l'alimentation en air est utilisé.In addition, to control the flow of injected air, a flow meter (not shown) between the 2nd inlet of the
Le dispositif de génération comprend également un agitateur 4 qui est par exemple du type Vortex Génius 3®. L'agitateur 4 comprend un logement pour maintenir le système de dispersion via le récipient inférieur 1.The generation device also comprises an
L'agitateur 4 permet de mettre en rotation le système de dispersion.The
De manière avantageuse, le canal 3 est agencé par rapport au récipient supérieur 2 pour que le système de dispersion puisse avoir un mouvement rotationnel sans être gêné par celui-ci.Advantageously, the
Ainsi, comme on le comprend, l'arrivée du débit d'air se fait au moyen du canal 3 qui est vertical et qui plonge directement dans le récipient inférieur 1 et qui permet de transporter les particules mises en suspension, grâce à l'agitation de la poudre P provoquée par l'agitateur 4 dans le récipient inférieur 1, vers la sortie 2c.Thus, as understood, the arrival of the air flow is by means of the
Pour assurer l'étanchéité au niveau de l'orifice d'entrée 2e, le dispositif de génération comprend un élément d'étanchéité 5 pour assurer l'étanchéité entre le canal 3 et le contour de l'orifice 2e.To seal at the
Le canal 3 est notamment solidaire du récipient supérieur 2.The
De manière avantageuse, l'orifice de sortie 2c est disposé suffisamment loin de l'extrémité du canal 3 plongeant dans le récipient inférieur.Advantageously, the
En outre, l'orifice de sortie 2c doit être situé dans la partie où la section du récipient supérieur est la plus grande car c'est cette section qui est utilisée pour calculer les vitesses dans le système et qui détermine la taille des particules sélectionnées (voir ci-après).In addition, the
Afin de pouvoir sélectionner une certaine taille de particules, le récipient supérieur 2 est en outre dimensionné d'une certaine manière. En effet, en fonction des dimensions et de la forme de ce dernier on peut sélectionner des particules ayant une certaine granulométrie.In order to be able to select a certain particle size, the
La forme conique du récipient supérieur 2 permet d'obtenir un écoulement stable lors du passage de l'aérosol par la base supérieure 2b en liaison avec le récipient inférieur 1.The conical shape of the
Le diamètre de la base supérieure 2a permet d'imposer une vitesse d'écoulement ascendant spécifique limitant l'extraction des particules ayant un diamètre aérodynamique supérieur à une valeur critique définit par la taille de la base supérieure 2a et le débit d'air injecté dans le système par le canal 3.The diameter of the
De manière préférée, le récipient supérieur 2 est tel que la partie intermédiaire 2d est convergente entre la base supérieure 2a et la base inférieure. Le récipient supérieur 2 est dans ce cas conique. C'est en particulier la section interne du récipient supérieur 2 qui va permettre de contrôler la taille maximale des particules de l'aérosol généré.Preferably, the
Ainsi, en ayant une partie intermédiaire 2d convergente entre la base supérieure 2a et la base inférieure 2b la section interne s'élargie de la base inférieure 2b vers la base supérieure 2b du récipient supérieur 2.Thus, by having an
Pour favoriser la mise en suspension des particules dans le récipient inférieur 1, ce dernier présente un fond ayant une section hémisphériqueTo promote the suspension of the particles in the lower container 1, the latter has a bottom having a hemispherical section
Une telle section hémisphérique présente en outre l'avantage d'être facilement nettoyable (pas d'angle vif).Such a hemispherical section has the further advantage of being easily cleaned (no sharp angle).
Par ailleurs, cette section hémisphérique est permet de bien adapter le récipient inférieur 1 à l'agitateur 4.Furthermore, this hemispherical section is suitable for adapting the lower container 1 to the
En outre, toujours pour favoriser la mise en suspension des particules, entre la base inférieure du récipient supérieur 2 et le récipient inférieur 1 on a un changement de section pour favoriser la mise en suspension dans le récipient inférieur 1. En particulier, le récipient inférieur présente une section plus large que la base inférieure du récipient supérieur 2.In addition, still to promote the suspension of the particles, between the lower base of the
De cette façon, un tel récipient inférieur 1 combiné à une section interne du récipient supérieur 2 convergente de la base supérieure 2a à la base inférieure 2b et au canal 3 qui amène directement l'air dans le récipient inférieur 1 permet de confiner la mise en suspension des particules dans le récipient inférieur 1.In this way, such a lower container 1 combined with an inner section of the
En outre, pour faciliter le dépôt de poudre P dans le récipient inférieur 1, le récipient inférieur 1 est amovible par rapport au récipient supérieur 2.In addition, to facilitate the deposition of powder P in the lower container 1, the lower container 1 is removable relative to the
Enfin il est possible de mélanger la poudre avec des billes en bronze ou en cuivre pour contribuer à la dispersion des particules.Finally it is possible to mix the powder with bronze or copper balls to contribute to the dispersion of the particles.
Grâce au dispositif de génération d'un aérosol ci-dessus décrit il est possible de générer un aérosol ayant des propriétés contrôlées.With the aerosol generating device described above it is possible to generate an aerosol having controlled properties.
Par exemple pour générer un aérosol d'alumine à partir d'une poudre d'alumine dont le diamètre médian des grains est de 0,65 µm, le dispositif de génération présente les paramètres suivants: débit d'air d'alimentation compris entre 0,1 L/min et 0,5 L/min ; variabilité de la concentration inférieure à 5 % sur une heure de production.For example, to generate an alumina aerosol from an alumina powder whose median grain diameter is 0.65 μm, the generation device has the following parameters: feed air flow rate between 0 , 1 L / min and 0.5 L / min; concentration variability less than 5% over one hour of production.
Claims (9)
- A device for generating an aerosol with a controlled grain size distribution, from a powder, the device comprising:- a system for dispersing (1, 2) particles comprising:∘ a lower container (1) referred to as a production area adapted to receive a powder (P);∘ an upper container (2) referred to as a selection area comprising an upper base (2a); an inlet port (2e); a lower base (2b) in aeraulic connection with the lower container (1); an intermediate part (2d) between the upper base (2a) and the lower base (2b); an outlet port (2c) disposed at the upper part of the upper base (2a);
the device being characterised in that it further comprises:- a channel (3) plunging from the inlet port (2e) down into the lower container (1) to directly convey air in said lower container (1), the inner section of the channel (3) being sized to obtain a turbulent air jet in the lower container (1);- a stirrer (4) comprising a housing adapted to accommodate the lower container (1) and rotate the dispersion system (1, 2). - The device according to claim 1, wherein the upper container (2) has a longitudinal symmetry axis along which the channel (3) extends.
- The device according to one of the preceding claims, wherein the upper container (2) is sized as a function of the desired grain size distribution for the aerosol.
- The device according to one of the preceding claims, wherein the inlet port (2e) is on the upper base (2a) and wherein the outlet port (2c) is on the intermediate part (2d).
- The device according to one of the preceding claims, wherein the intermediate part (2d) is converging between the upper base (2a) and the lower base (2b).
- The device according to one of the preceding claims, wherein the lower container (1) has a hemispheric section.
- The device according to one of the preceding claims, wherein the lower container (1) is removable with respect to the upper container (2).
- The device according to one of the preceding claims, further comprising a sealing element (5) surrounding the channel (3) to provide sealing between the channel and the contour of the inlet port (2e).
- A method for generating an aerosol by means of a device according to one of the preceding claims comprising the following steps:- disposing a powder (P) in the lower container (1);- bringing air by means of a channel (3) in the lower container (1) to suspense particles coming from the powder (P) to generate an aerosol;- stirring/rotating the generation system by means of a stirrer (4);- recovering the aerosol thus generated through the outlet port (2c).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1162079A FR2984179B1 (en) | 2011-12-20 | 2011-12-20 | DEVICE FOR GENERATING A CONTROLLED GRANULOMETRY AEROSOL |
PCT/EP2012/076309 WO2013092816A1 (en) | 2011-12-20 | 2012-12-20 | Device for generating an aerosol with a controlled particle size |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2794117A1 EP2794117A1 (en) | 2014-10-29 |
EP2794117B1 true EP2794117B1 (en) | 2015-12-16 |
Family
ID=47428647
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP12805701.5A Active EP2794117B1 (en) | 2011-12-20 | 2012-12-20 | Device for generating an aerosol with a controlled particle size |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP2794117B1 (en) |
FR (1) | FR2984179B1 (en) |
WO (1) | WO2013092816A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5831857B2 (en) * | 2012-01-24 | 2015-12-09 | 株式会社サンギ | Powder dispersion device, fine powder production method |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
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US3472430A (en) * | 1966-06-06 | 1969-10-14 | Nat Distillers Chem Corp | Method and apparatus for producing a dust cloud |
-
2011
- 2011-12-20 FR FR1162079A patent/FR2984179B1/en not_active Expired - Fee Related
-
2012
- 2012-12-20 WO PCT/EP2012/076309 patent/WO2013092816A1/en active Application Filing
- 2012-12-20 EP EP12805701.5A patent/EP2794117B1/en active Active
Also Published As
Publication number | Publication date |
---|---|
FR2984179B1 (en) | 2014-06-20 |
FR2984179A1 (en) | 2013-06-21 |
WO2013092816A1 (en) | 2013-06-27 |
EP2794117A1 (en) | 2014-10-29 |
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