WO1998031970A1 - Method for treating air for passenger space air-conditioning - Google Patents
Method for treating air for passenger space air-conditioning Download PDFInfo
- Publication number
- WO1998031970A1 WO1998031970A1 PCT/FR1998/000076 FR9800076W WO9831970A1 WO 1998031970 A1 WO1998031970 A1 WO 1998031970A1 FR 9800076 W FR9800076 W FR 9800076W WO 9831970 A1 WO9831970 A1 WO 9831970A1
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- WIPO (PCT)
- Prior art keywords
- air
- liquid
- cleaning system
- air cleaning
- reactor
- Prior art date
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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
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
- F24F8/117—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using wet filtering
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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
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
- F24F8/117—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using wet filtering
- F24F8/133—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using wet filtering by direct contact with liquid, e.g. with sprayed liquid
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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
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
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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
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
- F24F8/15—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering by chemical means
- F24F8/158—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering by chemical means using active carbon
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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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Definitions
- the present invention is a compact air purification system, designed more particularly to provide healthy and deodorized ambient air from air contaminated by exhaust gases, cigarettes, etc.
- compact interior air treatment systems use filters with a porous structure, in order to retain dust and aerosols or activated carbon in the dry process. These systems have reduced efficiencies and are limited to certain types of pollutants. They present a risk of clogging. Filters with a porous structure are effective only on particles and from a given diameter. Activated carbon filters are only effective on certain vapors and odors. Semi-humid systems have been envisaged, the principle being to pass the stale air over a filtering or fibrous medium humidified by an absorbent liquid solution. In the system described in patent WO 96/20097, a tank filled with fibers of hollow structure and large contact surface, moistened by an absorption reagent is used. This invention applies rather to the deodorization of an internal, confined atmosphere.
- wet processes using washing towers in which the reagents are sprayed against the current are versatile and effective. They are widely used for treating atmospheric emissions in the chemical industry, combustion plants and incinerators. These systems which spray reagents in washing towers, against the flow of stale air, are however not very suitable for miniaturization.
- the gas can also be passed through the liquid; this principle is used in industry, for the treatment of air loaded with solid or liquid suspended matter.
- the principles of bringing air into contact with water are the suction of air through a vortex, a venturi effect, or any means of crossing the flow of liquids and gases.
- the principle is notably widely used for the purification of air from paint booths.
- the water jet pump which is a use of the venturi effect, has been envisaged as a means of dedusting, in various settings, in particular for vacuum cleaners.
- the present invention belongs to the latter range of methods.
- the object of the invention is more particularly to treat polluted air in a single operation, with a compact device, with low energy consumption and limited maintenance, in order to provide healthy and breathable air.
- the specifications of the invention are: • Aspirating air which can be polluted by a wide spectrum of polluting compounds,
- the system described below is intended more specifically to treat conditioned interior air, whether to purify outside make-up air, polluted by exhaust gases or indoor air in recycling, contaminated by fumes and smells of cigarettes. It meets the specifications described above, however, from the means described in the invention, It is possible to produce systems which can be used for any type of treatment of stale air to be breathed. For example, without limitation: purify the compressed air from scuba or any breathing apparatus, before the compressor, treat the air in a "smoking" area in an air-conditioned room, treat the make-up air in an air-conditioned room during peaks of pollution, for people with fragile conditions respiratory system. Finally, this invention can also be adapted to purify any type of polluted air, even heavily loaded, but at low flow and when a compact system, not requiring significant maintenance is desired,
- Fig. 1 Single line diagram of the entire system.
- Fig. 2 Schematic axial section of the reactor, in which the water jet pump is fully submerged
- Fig. 3 System for lining the reactor body, with a perforated plate.
- the invention provides a solution to the above problem by using a system for extracting stale air by means of a liquid jet pump.
- the liquid producing the jet itself being the purification reagent used in a closed circuit.
- the system includes:
- the recirculation means for the operation of the closed circuit,
- the overflow is either pumped directly by the recirculation pump (6), or directed by gravity flow (7) into a reagent tank (8), where a submerged pump (9) is installed, which replenishes the recirculation pump (6 ).
- the air to be treated is drawn in directly by the liquid jet pump. It is taken up, after degassing, in the upper part of the reactor, directly by the cabin air conditioning system.
- the flow rate of the purification system can be increased and regulated by means of an air booster upstream of the suction.
- the basic reagent recommended is an aqueous medium, preferably an alkaline medium, which fixes the oxides of sulfur, nitrogen and carbon, captures the aerosols, dissolves the hydrocarbons,
- Powdered activated carbon is added to adsorb hydrocarbons, aldehydes and other odorous compounds which may be released by the reagent.
- Optimal efficiency is obtained by using a pump provided with a jet breaker in its lower part (10) and by directing the jet towards the base of a reactor of cylindrical shape (1 1), thus uniformly distributing the bubbles of air in the reactor and avoiding increasing the size of the air bubbles by melting them.
- the efficiency is also increased by increasing the contact time in the reactor, before degassing in the upper part, A filling with perforated plates or inclined strips allows this effect to be obtained,
- a make-up air treatment system for a passenger compartment. It can be housed in a hood and provide purified make-up air for passenger breathing, even from air heavily polluted by exhaust gases or cigarette smoke. It includes a reagent tank separate from the reactor, The stale air is sucked in by the air inlet (1) from the water jet pump (2), which is immersed in the reactor (3). Its axis is superimposed on the vertical axis (13) of the cylindrical reactor. The suction of the water jet pump (14) is connected by a pipe to an orifice located on the external wall of the reactor (15). The jet is directed vertically, downwards, on the lower horizontal wall of the cylinder (1 1). An overflow (5) is located in the upper part of the reactor.
- the reactor On the upper horizontal wall (16) there is an orifice (1 7) which collects the degassed air at the surface of the reagent (4) and the upper orifice for connection of the liquid inlet to the water jet pump (18).
- An orifice and a drain valve are provided in the lower part of the tank (19).
- the reactor has in its middle part a macroporous packing hermetically applied against the walls of the cylinder.
- This lining (12) is intended to slow the upward movement of the air bubbles by interposing on their trajectory a series of baffles, before arriving at the surface of the liquid, It is located between the lower part of the jet pump d water (12) and the overflow (13),
- An example of lining with perforated cellular etching plates is given on p 8, and fig 4. NB
- the lining is not essential for the operation of the device, however, it improves the efficiency, without significantly increasing the pressure drop.
- the reactor overflow (5) flows by gravity into a reagent tank (8), located in the lower position relative to the reactor.
- a submerged pump (9) is located in the tank. This pump ensures both the mixing of the reagent and the raising of the liquid to the reactor.
- a hole in the upper part of the reservoir (21) allows the filling of reagent (water, soda, activated carbon, or others, ).
- a drain valve is provided in the lower part (22).
- the discharge pipe (23) of the submerged pump supplies the water jet pump, either directly or through a so-called "jockey” pump (6 ) whose function is to restore sufficient pressure to the inlet of the water jet pump (18).
- the reactive liquid has several functions:
- Powdered activated carbon is added to the solution, in order to capture residual odors and increase the capacity to fix unburnt volatile hydrocarbons, aldehydes and other volatile odorous products weakly fixed by the alkaline solution.
- the water jet pump used consists of a water inlet pipe (18), followed by a reduction in diameter creating a pressure drop, then by a conical throttle accelerating the jet (24) . This is sent into a pipe with a diameter greater than the jet and widening towards a tubular end part (25). Upstream of this pipe, in the vacuum zone (14), is the air intake.
- the internal lining of the reactor is intended to prevent bubbles from rising vertically and rapidly in a straight line. This filling must create baffles which will slow down this ascent. In any case, the packing must not create a significant loss of load, nor passage through pores or orifices of small diameters which would risk clogging and block the free rise of bubbles.
- This lining can be produced from stacks of perforated cell plates or grids made up of strips inclined with respect to the horizontal (12).
- Fig. 3 describes a stack made up of plates (26), the underside of which is made up of cells of square shape (27) in plan view and of hollow triangular shape in cross section (28), the top of the triangle, facing towards top, is extended by a perforation (29). The organization of the stack, by shifting the orifices relative to the vertical, causes a movement of the bubbles, in a sawtooth fashion, the result of which is vertical. By this device, there is an increase in contact time, without significant pressure drop.
- a booster can be added to the air supply (1), which allows the flow to be increased and regulated.
- the ventilation system of the passenger compartment air conditioning also allows, to a lesser extent, to increase and vary the flow.
- the purifying yield will however decrease at the same time as the increase in the air flow / purifying reagent flow ratio.
- the system can also be modified in that the bringing into contact between the air and the purifying liquid is carried out by means of a booster assembly - injection pipe in the reactor, and suction in the upper part.
- the purifying liquid being kept in circulation in a closed circuit, only to ensure mixing and homogeneity.
- the injection rod is provided at its end with means for distributing fine bubbles at the base of the reactor.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
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Abstract
The invention concerns a method for treating polluted air in a single operation, using a compact appliance, with low energy consumption and limited maintenance, for supplying clean and breathable air. The invention uses a system for sucking the stale air by means of a pump with liquid jet, said jet producing liquid being itself the purifying reagent operating in close circuit. The system comprises an air intake (1), means for recycling, for operating in close circuit (6, 9) a water jet pump (2), sucking the liquid and producing the reactive air-liquid contact, a reactor (3), in which the reactive air-liquid contact is continued, the degassing (4) and the recuperating of the overflow (5). The air outlet (17) is sucked by the air conditioning system. The recommended base reagent is an aqueous medium, preferably alkaline, which fixes sulphur, nitrogen and carbon oxides, captures aerosols, dissolves hydrocarbons. Activated carbon in powder form is added so as to absorb the hydrocarbons, aldehydes and other odorous compounds which may be salted out by the reactive liquid.
Description
SYSTEME DE TRAITEMENT D'AIR POUR LA CLIMATISATION D'HABITACLES AIR TREATMENT SYSTEM FOR AIR CONDITIONING
La présente invention est un système compact de purification de l'air, conçu plus particulièrement pour fournir un air d'ambiance sain et désodorisé à partir d'air souillé par les gaz d'échappement, cigarettes, etc..The present invention is a compact air purification system, designed more particularly to provide healthy and deodorized ambient air from air contaminated by exhaust gases, cigarettes, etc.
ÉTAT DE LA TECHNIQUESTATE OF THE ART
D'une manière générale, les systèmes compacts de traitement d'air d'-habitacle utilisent des filtres à structure poreuse, afin de retenir les poussières et aérosols ou du charbon actif en voie sèche. Ces systèmes ont des efficacités réduites et sont limités à certains types de polluants. Ils présentent un risque de colmatage. Les filtres à structure poreuse sont efficaces uniquement sur les particule et à partir d'un diamètre donné. Les filtres à charbon actif sont efficaces uniquement sur certaines vapeurs et odeurs. Des systèmes semi-humides ont été envisagés , le principe étant de faire passer l'air vicié sur un milieu filtrant ou fibreux humidifié par une solution liquide absorbante. Dans Le système décrit dans le brevet WO 96/20097, un réservoir garnie de fibres à structure creuse et grande surface de contact, humidifiée par un réactif d'absorption est utilisé. Cette invention s'applique plutôt à la désodorisation d'une atmosphère interne, confinée.In general, compact interior air treatment systems use filters with a porous structure, in order to retain dust and aerosols or activated carbon in the dry process. These systems have reduced efficiencies and are limited to certain types of pollutants. They present a risk of clogging. Filters with a porous structure are effective only on particles and from a given diameter. Activated carbon filters are only effective on certain vapors and odors. Semi-humid systems have been envisaged, the principle being to pass the stale air over a filtering or fibrous medium humidified by an absorbent liquid solution. In the system described in patent WO 96/20097, a tank filled with fibers of hollow structure and large contact surface, moistened by an absorption reagent is used. This invention applies rather to the deodorization of an internal, confined atmosphere.
Des procédés que l'on peut qualifier également de semi-humides dans lesquels un filtre est imprégné d'un réactif ont été envisagés pour des hottes d'aspiration de cuisines ou laboratoires.Processes which can also be described as semi-humid in which a filter is impregnated with a reagent have been envisaged for extractor hoods in kitchens or laboratories.
Dans le traitement des effluents gazeux industriels, les procédés par voie humide utilisant des tours de lavage dans lesquelles les réactifs sont pulvérisés à contre-courant sont polyvalents et efficaces. Ils sont très largement utilisés pour les traitements de émissions atmosphériques dans l'industrie chimiques, les installations de combustion et les incinérateurs. Ces systèmes qui pulvérisent des réactifs dans des tours de lavage, à contre-courant de l'air vicié, se prêtent cependant assez peu à la miniaturisation.
Pour traiter un gaz contaminé par voie humide, on peut également faire passer le gaz dans le liquide; ce principe est utilisé dans l'industrie, pour le traitement d'air chargé en matières en suspension solides ou liquides. Les principes de mise en contact de l'air avec de l'eau sont l'aspiration d'air au travers d'un vortex,d'un effet de venturi, ou de tout moyen de croisement de flux de liquides et de gaz. Le principe est notamment largement utilisé pour l'épuration de l'air de cabines de peinture. La pompe à jet d'eau, qui est une uilisation de l'effet venturi, a été envisagée comme moyen de dépoussiérage, dans divers cadres, en particulier pour les aspirateurs. La présente invention appartient à cette dernière gamme de procédés.In the treatment of industrial gaseous effluents, wet processes using washing towers in which the reagents are sprayed against the current are versatile and effective. They are widely used for treating atmospheric emissions in the chemical industry, combustion plants and incinerators. These systems which spray reagents in washing towers, against the flow of stale air, are however not very suitable for miniaturization. To treat a contaminated gas wet, the gas can also be passed through the liquid; this principle is used in industry, for the treatment of air loaded with solid or liquid suspended matter. The principles of bringing air into contact with water are the suction of air through a vortex, a venturi effect, or any means of crossing the flow of liquids and gases. The principle is notably widely used for the purification of air from paint booths. The water jet pump, which is a use of the venturi effect, has been envisaged as a means of dedusting, in various settings, in particular for vacuum cleaners. The present invention belongs to the latter range of methods.
PROBLEME TECHNIQUE A RESOUDRETECHNICAL PROBLEM TO BE SOLVED
L'invention a plus particulièrement pour but de traiter un air pollué en une seule opération, par un appareil compact, à faible consommation d'énergie et maintenance limitée, pour fournir un air sain et respirable.The object of the invention is more particularly to treat polluted air in a single operation, with a compact device, with low energy consumption and limited maintenance, in order to provide healthy and breathable air.
Plus précisément, le cahier des charges de l'invention est : • Aspirer de l'air qui peut être pollué par un large spectre de composés polluants,More specifically, the specifications of the invention are: • Aspirating air which can be polluted by a wide spectrum of polluting compounds,
• Fournir un air d'appoint ou de recyclage sain pour le confort et la santé des personnes occupant l'habitacle.• Provide healthy make-up or recycling air for the comfort and health of the people occupying the passenger compartment.
• Concevoir un système compact pour être logeable, par exemple, sous un capot d'automobile, chaque réservoir n'occupant pas plus de place, par exemple, qu'un récipient de lave-glace.• Design a compact system to be accommodated, for example, under a car hood, each tank occupying no more space, for example, than a windshield washer container.
• Avoir une faible consommation électrique, par exemple, compatible avec l'alimentation électrique d'une automobile.• Have a low power consumption, for example, compatible with the power supply of an automobile.
• Ne pas demander de maintenance excessive, ne pas se colmater.• Do not ask for excessive maintenance, do not clog up.
Le système décrit ci-dessous est destiné plus particulièrement à traiter l'air d'habitacle climatisé, que ce soit pour épurer un air d'appoint extérieur, pollué par les gaz d'échappements ou un air intérieur en recyclage, vicié par les fumées et odeurs de cigarettes. Il répond au cahier des charges décrit ci- dessus, Toutefois, à partir des moyens décrits dans l'invention, Il est possible de réaliser des systèmes pouvant servir pour tout type de traitement de l'air vicié devant être respiré. Par exemple non limitatif : épurer l'air comprimé de
scaphandre autonome ou tout appareil respiratoire, avant le compresseur, traiter l'air d'une zone "fumeurs" dans un local climatisé, traiter l'air d'appoint d'une pièce climatisée lors de pointes de pollution, pour les personnes fragiles du système respiratoire. Enfin, cette invention peut également être adaptée pour épurer tout type d'air pollué, même fortement chargé, mais à faible débit et lorsqu'un système compact, ne demandant pas une maintenance importante est souhaité,
The system described below is intended more specifically to treat conditioned interior air, whether to purify outside make-up air, polluted by exhaust gases or indoor air in recycling, contaminated by fumes and smells of cigarettes. It meets the specifications described above, However, from the means described in the invention, It is possible to produce systems which can be used for any type of treatment of stale air to be breathed. For example, without limitation: purify the compressed air from scuba or any breathing apparatus, before the compressor, treat the air in a "smoking" area in an air-conditioned room, treat the make-up air in an air-conditioned room during peaks of pollution, for people with fragile conditions respiratory system. Finally, this invention can also be adapted to purify any type of polluted air, even heavily loaded, but at low flow and when a compact system, not requiring significant maintenance is desired,
EXPOSE DE L'INVENTIONSTATEMENT OF THE INVENTION
Liste des figures annexées se rapportant à la description :List of attached figures relating to the description:
Fig. 1 : Schéma unifilaire de l'ensemble du système.Fig. 1: Single line diagram of the entire system.
Fig. 2 : Coupe axiale schématique du réacteur, dans lequel la pompe à jet d'eau est entièrement immergée,Fig. 2: Schematic axial section of the reactor, in which the water jet pump is fully submerged,
Fig. 3 : Système de garnissage du corps du réacteur, à plaque perforée.Fig. 3: System for lining the reactor body, with a perforated plate.
L'invention fournit une solution au problème ci-dessus en utilisant un système d'aspiration de l'air vicié au moyen d'une pompe à jet de liquide. Le liquide produisant le jet étant lui-même le réactif d'épuration mis en oeuvre en circuit fermé.The invention provides a solution to the above problem by using a system for extracting stale air by means of a liquid jet pump. The liquid producing the jet itself being the purification reagent used in a closed circuit.
Le système comprend :The system includes:
• une arrivée d'air (1 ),• an air intake (1),
• les moyens de recirculation, pour le fonctionnement du circuit fermé,The recirculation means, for the operation of the closed circuit,
• une pompe à jet d'eau (2), aspirant le liquide et réalisant le contact air- réactif,• a water jet pump (2), sucking up the liquid and making the air-reactive contact,
• un réacteur (3), dans lequel se poursuit le contact air-liquide, le dégazage (4) et la récupération de la surverse (5),• a reactor (3), in which the air-liquid contact, the degassing (4) and the recovery of the overflow (5) continue,
La surverse est soit repompée directement par la pompe de recirculation (6), soit dirigée par écoulement gravitaire (7) dans un réservoir de réactif (8), où est installée une pompe immergée (9), qui réalimente la pompe de recirculation (6).The overflow is either pumped directly by the recirculation pump (6), or directed by gravity flow (7) into a reagent tank (8), where a submerged pump (9) is installed, which replenishes the recirculation pump (6 ).
L'air à traiter est aspiré directement par la pompe à jet de liquide. Il est repris, après dégazage, dans la partie supérieure du réacteur, directement par le système de climatisation de la cabine.The air to be treated is drawn in directly by the liquid jet pump. It is taken up, after degassing, in the upper part of the reactor, directly by the cabin air conditioning system.
Le débit du système épuratoire peut être augmenté et régulé au moyen d'un surpresseur d'air en amont de l'aspiration.
Le réactif de base préconisé est un milieu aqueux, de préférence alcalin, qui fixe les oxydes de soufre, d'azote et de carbone, capte les aérosols, dissout les hydrocarbures ,The flow rate of the purification system can be increased and regulated by means of an air booster upstream of the suction. The basic reagent recommended is an aqueous medium, preferably an alkaline medium, which fixes the oxides of sulfur, nitrogen and carbon, captures the aerosols, dissolves the hydrocarbons,
Du charbon actif en poudre est ajouté afin d'adsorber les hydrocarbures, aldéhydes et autres composés odorants qui risquent d'être relargués par le réactif.Powdered activated carbon is added to adsorb hydrocarbons, aldehydes and other odorous compounds which may be released by the reagent.
Ces deux réactifs peuvent être utilisés à des concentrations très élevées, afin d'augmenter l'efficacité du procédé, mais surtout de fixer, dans un faible volume, une quantité importante de composés polluants, avant saturation du réactif,These two reagents can be used at very high concentrations, in order to increase the efficiency of the process, but above all to fix, in a small volume, a large quantity of polluting compounds, before saturation of the reagent,
Une efficacité optimale est obtenue en utilisant une pompe munie d'un brise-jet dans sa partie inférieure (10) et en dirigeant le jet vers la base d'un réacteur de forme cylindrique (1 1 ) , répartissant ainsi uniformément les bulles d'air dans le réacteur et évitant l'augmentation de la taille des bulles d'air par fusion de celles-ci.Optimal efficiency is obtained by using a pump provided with a jet breaker in its lower part (10) and by directing the jet towards the base of a reactor of cylindrical shape (1 1), thus uniformly distributing the bubbles of air in the reactor and avoiding increasing the size of the air bubbles by melting them.
L'efficacité est également augmentée en augmentant le temps de contact dans le réacteur, avant le dégazage en partie supérieure, Un garnissage par des plaques perforées ou des lamelles inclinées permet d'obtenir cet effet,The efficiency is also increased by increasing the contact time in the reactor, before degassing in the upper part, A filling with perforated plates or inclined strips allows this effect to be obtained,
DESCRIPTION DETAILLEE DE L'INVENTIONDETAILED DESCRIPTION OF THE INVENTION
La description détaillée présentée ci-dessous concerne plus particulièrement la réalisation d'un système de traitement d'air d'appoint pour un habitacle automobile. Elle peut se loger dans un capot et fournir un air d'appoint épuré pour la respiration des passagers, même à partir d'air fortement pollué par des gaz d'échappement ou de la fumée de cigarettes. Elle inclut un réservoir de réactif séparé du réacteur,
L'air vicié est aspiré par I' arrivée d'air (1 ) de la pompe à jet d'eau (2), qui est immergée dans le réacteur (3). Son axe est superposé avec l'axe vertical (13) du réacteur cylindrique. L'aspiration de la pompe à jet d'eau (14) est reliée par une conduite à un orifice situé sur la paroi externe du réacteur (15). Le jet est dirigé verticalement, vers le bas, sur la paroi horizontale inférieure du cylindre (1 1 ). Une surverse (5) est située en partie haute du réacteur.The detailed description presented below relates more particularly to the production of a make-up air treatment system for a passenger compartment. It can be housed in a hood and provide purified make-up air for passenger breathing, even from air heavily polluted by exhaust gases or cigarette smoke. It includes a reagent tank separate from the reactor, The stale air is sucked in by the air inlet (1) from the water jet pump (2), which is immersed in the reactor (3). Its axis is superimposed on the vertical axis (13) of the cylindrical reactor. The suction of the water jet pump (14) is connected by a pipe to an orifice located on the external wall of the reactor (15). The jet is directed vertically, downwards, on the lower horizontal wall of the cylinder (1 1). An overflow (5) is located in the upper part of the reactor.
Sur la paroi horizontale supérieure (16) se trouvent un orifice (1 7) qui récupère l'air dégazé en surface du réactif (4) et l'orifice supérieur de connexion de l'arrivée de liquide sur la pompe à jet d'eau (18). Un orifice et une vanne de vidange sont prévus en partie inférieure du réservoir (19). Le réocteur comporte dans sa partie médiane un garnissage macroporeux hermétiquement appliqué contre les parois du cylindre. Ce garnissage (12) est destiné à ralentir le mouvement ascensionnel des bulles d'air en interposant sur leur trajectoire une série de chicanes, avant d'arriver à la surface du liquide, Il est situé entre la partie inférieure de la pompe à jet d'eau (12) et la surverse (13), Un exemple de garnissage par plaques à gravures cellulaires perforées est donné en p 8, et fig 4. N.B. Le garnissage n'est pas indispensable au fonctionnement du dispositif, cependant, il améliore le rendement, sans augmenter significativement la perte dé charge.On the upper horizontal wall (16) there is an orifice (1 7) which collects the degassed air at the surface of the reagent (4) and the upper orifice for connection of the liquid inlet to the water jet pump (18). An orifice and a drain valve are provided in the lower part of the tank (19). The reactor has in its middle part a macroporous packing hermetically applied against the walls of the cylinder. This lining (12) is intended to slow the upward movement of the air bubbles by interposing on their trajectory a series of baffles, before arriving at the surface of the liquid, It is located between the lower part of the jet pump d water (12) and the overflow (13), An example of lining with perforated cellular etching plates is given on p 8, and fig 4. NB The lining is not essential for the operation of the device, however, it improves the efficiency, without significantly increasing the pressure drop.
La surverse (5) du réacteur s'écoule par gravité dans un réservoir de réactif (8), situé en position inférieure par rapport au réacteur, Une pompe immergée (9) est située dans le réservoir. Cette pompe assure à la fois le mélange du réactif et le relevage du liquide vers le réacteur, . Un orifice en partie supérieure du réservoir (21 ) permet d'effectuer le remplissage de réactif (Eau, soude, charbon actif, ou autres, ... ). Une vanne de vidange est prévue en partie inférieure (22), La conduite de refoulement (23) de la pompe immergée alimente la pompe à jet d'eau, soit directement soit par l'intermédiaire d'une pompe dite "jockey" (6) dont la fonction est de redonner une pression suffisante à l'entrée de la pompe à jet d'eau (18).
Le liquide réactif a plusieurs fonctions :The reactor overflow (5) flows by gravity into a reagent tank (8), located in the lower position relative to the reactor. A submerged pump (9) is located in the tank. This pump ensures both the mixing of the reagent and the raising of the liquid to the reactor. A hole in the upper part of the reservoir (21) allows the filling of reagent (water, soda, activated carbon, or others, ...). A drain valve is provided in the lower part (22). The discharge pipe (23) of the submerged pump supplies the water jet pump, either directly or through a so-called "jockey" pump (6 ) whose function is to restore sufficient pressure to the inlet of the water jet pump (18). The reactive liquid has several functions:
• L'entraînement de l'air lors du passage dans la pompe à jet de liquide.• Air entrainment when passing through the liquid jet pump.
• Le contact avec les composés polluants. • La neutralisation, la dissolution, la fixation des polluants ;• Contact with polluting compounds. • Neutralization, dissolution, fixation of pollutants;
• le stockage de ces composés dans le liquide réactif, jusqu'à la saturation de celui-ci;• storage of these compounds in the reactive liquid, until the latter is saturated;
• La modification de la tension superficielle, qui provoquera la réduction de la taille des bulles et donc augmentera la surface de contact et l'efficacité du système.• The modification of the surface tension, which will cause the reduction of the size of the bubbles and therefore will increase the contact surface and the efficiency of the system.
Pour l'exemple d'utilisation pris en compte, et pour remplir les fonctions indiquées ci-dessus, le mélange suivant est préconisé :For the example of use taken into account, and to fulfill the functions indicated above, the following mixture is recommended:
Une solution concentrée de soude en milieu aqueux, ou toute autre solution alcaline, à laquelle est ajouté du charbon actif en poudre,A concentrated solution of sodium hydroxide in an aqueous medium, or any other alkaline solution, to which powdered activated carbon is added,
• L'eau produit l'effet de captage et fixation par dissolution des vapeurs et gaz tels qu' oxydes d'azote de carbone, de soufre, ozone, etc..,)• Water produces the capture and fixing effect by dissolving vapors and gases such as carbon nitrogen oxides, sulfur, ozone, etc.,)
• L'utilisation d'une solution aqueuse alcaline augmente l'efficacité, et la capacité de fixation des composés décrits ci-dessus , par réaction de neutralisation. Elle permet également de fixer les hydrocarbures sous formes d'aérosols ou de vapeurs, les goudrons, les huiles et goudrons, par augmentation de leur solubilité.• The use of an alkaline aqueous solution increases the efficiency, and the fixing capacity of the compounds described above, by neutralization reaction. It also makes it possible to fix hydrocarbons in the form of aerosols or vapors, tars, oils and tars, by increasing their solubility.
Il est important de préciser que le dispositif est efficace sans soude, qu'il est plus efficace avec la soude et que la capacité de fixation des produits cités plus haut est proportionnelle à la quantité de soude mise en solution. Une concentration élevée en soude a pour seul inconvénient d'entraîner l'obligation de manipuler un liquide corrosif pour le remplissage.It is important to specify that the device is effective without soda, that it is more effective with soda and that the fixing capacity of the products mentioned above is proportional to the amount of soda dissolved. The only drawback of a high sodium hydroxide concentration is the need to handle a corrosive liquid for filling.
• Du charbon actif en poudre est ajouté dans la solution, afin de capter les odeurs résiduelles et d'augmenter la capacité à fixer les hydrocarbures volatils imbrûlés, les aldéhydes et autres produits volatils odorants et faiblement fixés par la solution alcaline.• Powdered activated carbon is added to the solution, in order to capture residual odors and increase the capacity to fix unburnt volatile hydrocarbons, aldehydes and other volatile odorous products weakly fixed by the alkaline solution.
II est également possible d'utiliser l'invention sans charbon actif en poudre, en tant que prétraitement avant un filtre à charbon actif en poudre. Les deux étapes de traitement sont alors complémentaires. La durée de vie du filtre à charbon actif par voie sèche sera augmentée, si le sytème présenté est utilisé
en αmont. De plus, la gamme d'application du système global constitué par la présente invention, suivie d'un filtre à charbon actif est considérablement étendue par rapport à un filtre à charbon actif seul.It is also possible to use the invention without powdered activated carbon, as a pretreatment before a powdered activated carbon filter. The two processing steps are then complementary. The service life of the dry activated carbon filter will be increased, if the system presented is used in αmont. In addition, the range of application of the overall system constituted by the present invention, followed by an activated carbon filter is considerably extended compared to an active carbon filter alone.
La pompe à jet d'eau utilisée est constituée d'un conduite d' arrivée d'eau, (18), suivie d'une réduction de diamètre créant une perte de charge, puis d'un étranglement conique accélérant le jet (24). Celui-ci est envoyé dans une conduite de diamètre supérieur au jet et s'évasant vers une partie finale tubulaire (25). En amont de cette conduite, dans la zone de dépression (14), se trouve la prise d'air. Un brise jet (10), situé dans la partie tubulaire divise le jet, créant l'appel d'air en amont et la mise en contact air-eau.The water jet pump used consists of a water inlet pipe (18), followed by a reduction in diameter creating a pressure drop, then by a conical throttle accelerating the jet (24) . This is sent into a pipe with a diameter greater than the jet and widening towards a tubular end part (25). Upstream of this pipe, in the vacuum zone (14), is the air intake. A jet breaker (10), located in the tubular part, divides the jet, creating the upstream air draw and the air-water contact.
Le garnissage interne du réacteur est destiné à éviter que les bulles ne remontent verticalement et rapidement en ligne droite. Ce garnissage doit créer des chicanes qui ralentiront cette remontée. En aucun cas, le garnissage ne devra créer de perte de charges importantes, ni de passage par des pores ou orifices de faibles diamètres qui risqueraient de s'obstruer et de bloquer la remontée libre de bulles. Ce garnissage peut être réalisé à partir d'empilements de plaques cellulaires perforées ou de grilles constituées de lamelles inclinées par rapport à l'horizontale (12). La fig. 3 décrit un empilement constitué de plaques (26), dont la face inférieure est constituée de cellules de forme carrée (27) en vue en plan et de forme creuse triangulaire en coupe transversale (28), dont le sommet du triangle, tourné vers le haut, est prolongé d'une perforation (29). L'organisation de l'empilement, en décalant les orifices par rapport à la verticale, provoque un mouvement des bulles, en dents de scie, dont la résultante est verticale. Il y a par ce dispositif une augmentation du temps de contact, sans perte de charge sensible.The internal lining of the reactor is intended to prevent bubbles from rising vertically and rapidly in a straight line. This filling must create baffles which will slow down this ascent. In any case, the packing must not create a significant loss of load, nor passage through pores or orifices of small diameters which would risk clogging and block the free rise of bubbles. This lining can be produced from stacks of perforated cell plates or grids made up of strips inclined with respect to the horizontal (12). Fig. 3 describes a stack made up of plates (26), the underside of which is made up of cells of square shape (27) in plan view and of hollow triangular shape in cross section (28), the top of the triangle, facing towards top, is extended by a perforation (29). The organization of the stack, by shifting the orifices relative to the vertical, causes a movement of the bubbles, in a sawtooth fashion, the result of which is vertical. By this device, there is an increase in contact time, without significant pressure drop.
En tant que variante au système, on peut ajouter un surpresseur à l'arrivée d'air (1 ), ce qui permet d'augmenter et de réguler le débit. Le système de ventilation de la climatisation de l'habitacle permet également, dans une moindre mesure, de faire augmenter et varier le débit. Le rendement épuratoire va toutefois décroître en même temps que l'augmentation du rapport débit d'air / débit de réactif épuratoire.
Le système peut également être modifié en ce que la mise en contact entre l'air et le liquide épuratoire est réalisé au moyen d'un ensemble surpresseur - canne d'injection dans le réacteur, et aspiration en partie supérieure. Le liquide épuratoire étant maintenu en circulation en circuit fermé, uniquement pour en assurer le mélange et l'homogénéïté, La canne d'injection est munie en son extrémité de moyens de répartition de fines bulles à la base du réacteur.
As a variant of the system, a booster can be added to the air supply (1), which allows the flow to be increased and regulated. The ventilation system of the passenger compartment air conditioning also allows, to a lesser extent, to increase and vary the flow. The purifying yield will however decrease at the same time as the increase in the air flow / purifying reagent flow ratio. The system can also be modified in that the bringing into contact between the air and the purifying liquid is carried out by means of a booster assembly - injection pipe in the reactor, and suction in the upper part. The purifying liquid being kept in circulation in a closed circuit, only to ensure mixing and homogeneity. The injection rod is provided at its end with means for distributing fine bubbles at the base of the reactor.
Claims
REVENDICATIONS
1 - Système compact d'épuration d'air, adapté pour le traitement d'air d'habitacle, caractérisé en ce qu'il comprend ;1 - Compact air purification system, suitable for the treatment of cabin air, characterized in that it comprises;
• Les moyens de raccordement à une prise d'air (1 ),• The means of connection to an air intake (1),
• Une pompe à jet de liquide (2) aspirant l'air vicié, le liquide étant un réactif circulant en circuit fermé, grâce auquel il est possible de piéger un large éventail de composés polluants en une seule opération,• A liquid jet pump (2) sucking the stale air, the liquid being a reactant circulating in a closed circuit, thanks to which it is possible to trap a wide range of polluting compounds in a single operation,
• Un réacteur (3) dans lequel est injecté le jet ayant aspiré l'air vicié, muni d'une surverse (5) pour l'évacuation du liquide réactif et d'une cavité• A reactor (3) into which is injected the jet having sucked the stale air, provided with an overflow (5) for the evacuation of the reactive liquid and a cavity
- supérieure de dégazage de l'air épuré (4), • Les moyens de pompage et les conduites permettant de créer la circulation du liquide réactif avec la pression suffisante pour le fonctionnement du système de pompe à jet de liquide en circuit fermé,- upper degassing of purified air (4), • The pumping means and the pipes making it possible to create the circulation of the reactive liquid with sufficient pressure for the operation of the liquid jet pump system in closed circuit,
• Les moyens de raccordement de la sortie d'air épuré, à un système de ventilation (17),• The means of connection of the purified air outlet, to a ventilation system (17),
2 - Système d'épuration d'air selon la revendication 1 , caractérisé en ce qu'il envoie le jet de la pompe à jet de liquide verticalement sur la base horizontale (1 1 ) d'un réacteur cylindrique et répartit ainsi les bulles de gaz uniformément dans le réacteur avant qu'elles n'entament leur mouvement ascensionnel.2 - Air cleaning system according to claim 1, characterized in that it sends the jet of the liquid jet pump vertically on the horizontal base (1 1) of a cylindrical reactor and thus distributes the bubbles of gas uniformly in the reactor before they begin their upward movement.
3 - Système d'épuration d'air selon la revendication 1 caractérisé en ce que le réacteur contient, au dessus du point d'injection du jet, les moyen d'augmenter le temps de remontée des bulles dans le réservoir, pour une faible perte de charge, grâce à un garnissage (12) formant obstacle au mouvement vertical direct des bulles d'air vers la surface de dégazage.3 - Air cleaning system according to claim 1 characterized in that the reactor contains, above the point of injection of the jet, the means of increasing the time of rise of the bubbles in the tank, for a small loss load, thanks to a lining (12) forming an obstacle to the direct vertical movement of the air bubbles towards the degassing surface.
4 - Système d'épuration d'air selon la revendication 1 , caractérisé en ce que le circuit fermé comprend l'écoulement par gravité de la surverse (5) du liquide réactif dans un réservoir (8) dans lequel se trouve une pompe immergée (9) qui réalimente la pompe à jet de liquide (2).
5 - Système d'épuration d'air selon les revendications 1 et 4, caractérisé en ce qu' une pompe (6) située juste en amont de la pompe à jet de liquide redonne la pression nécessaire pour le fonctionnement optimal de celle-ci.4 - Air cleaning system according to claim 1, characterized in that the closed circuit comprises the flow by gravity of the overflow (5) of the reactive liquid in a tank (8) in which there is a submerged pump ( 9) which replenishes the liquid jet pump (2). 5 - Air cleaning system according to claims 1 and 4, characterized in that a pump (6) located just upstream of the liquid jet pump restores the pressure necessary for the optimal operation thereof.
6 - Système d'épuration d'air selon la revendication 1 , caractérisé en ce que le liquide réactif est une solution aqueuse, permettant de capter et de fixer dans la solution, par exemples non limitatifs, les oxydes de carbone, de soufre, d'azote, les aérosols d' huiles, les goudrons, les hydrocarbures imbrûlés...par un ensemble de phénomènes mettant en jeu notamment la capillarité, la migration par différence de concentration, la solubilisation.6 - Air cleaning system according to claim 1, characterized in that the reactive liquid is an aqueous solution, making it possible to capture and fix in the solution, for example nonlimiting, oxides of carbon, sulfur, d 'nitrogen, oil aerosols, tars, unburnt hydrocarbons ... by a set of phenomena involving in particular capillarity, migration by difference in concentration, solubilization.
7 - Système d'épuration d'air selon les revendications 1 et 6, caractérisé en ce que la solution aqueuse est alcaline et contient des ions hydroxides dont la valeur supérieure de concentration n'est pas limitée, permettant d'améliorer l'efficacité de la solution aqueuse, en particulier pour les oxydes de carbone, de soufre, d'azote et d'augmenter la capacité de rétention pour les composés précédemment cités par neutralisation ainsi que les aérosols d' huiles, et les goudrons, les hydrocarbures imbrûlés par solubilisation.7 - Air cleaning system according to claims 1 and 6, characterized in that the aqueous solution is alkaline and contains hydroxide ions whose higher value of concentration is not limited, allowing to improve the efficiency of the aqueous solution, in particular for the oxides of carbon, sulfur, nitrogen and to increase the capacity of retention for the compounds quoted previously by neutralization as well as the aerosols of oils, and the tars, the hydrocarbons unburnt by dissolution .
8 - Système d'épuration d'air selon l'ensemble des revendications 1 , 4, et 6, ou 1 , 4, 6 et 7 caractérisé en ce que le liquide réactif contient du charbon actif en poudre, permettant le traitement des hydrocarbures volatils, aldéhydes et autres composés odorants et leur fixation par adsorption dans le liquide réactif, jusqu'à saturation,8 - Air cleaning system according to all of claims 1, 4, and 6, or 1, 4, 6 and 7 characterized in that the reactive liquid contains powdered activated carbon, allowing the treatment of volatile hydrocarbons , aldehydes and other odorous compounds and their fixation by adsorption in the reactive liquid, until saturation,
9 - Système d'épuration d'air selon les revendications 1 , 6 et 7, caractérisé en ce qu'il est utilisé comme prétraitement avant l'utilisation d'un filtre à charbon actif en voie sèche.9 - Air cleaning system according to claims 1, 6 and 7, characterized in that it is used as pretreatment before the use of an activated carbon filter in the dry process.
10 - Système d'épuration d'air selon la revendication 1 , caractérisé en ce qu' un moyen de créer et régler une surpression située en amont de l'arrivée d'air de la pompe à jet de liquide, permet d'augmenter et de réguler le débit d'air .
10 - Air cleaning system according to claim 1, characterized in that a means of creating and adjusting an overpressure located upstream of the air inlet of the liquid jet pump, makes it possible to increase and regulate the air flow.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU59926/98A AU5992698A (en) | 1997-01-21 | 1998-01-16 | Method for treating air for passenger space air-conditioning |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9700652A FR2758612B1 (en) | 1997-01-21 | 1997-01-21 | COMPACT AND VERSATILE WET AIR TREATMENT SYSTEM FOR AIR CONDITIONING |
FR97/00652 | 1997-01-21 |
Publications (1)
Publication Number | Publication Date |
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WO1998031970A1 true WO1998031970A1 (en) | 1998-07-23 |
Family
ID=9502873
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR1998/000076 WO1998031970A1 (en) | 1997-01-21 | 1998-01-16 | Method for treating air for passenger space air-conditioning |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU5992698A (en) |
FR (1) | FR2758612B1 (en) |
WO (1) | WO1998031970A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20170010044A1 (en) * | 2013-12-11 | 2017-01-12 | Starklab | Device for producing a stream of air through a volume of liquid |
US20170320006A1 (en) * | 2014-11-06 | 2017-11-09 | Starklab | Device for producing and treating a gas stream through a volume of liquid, and facility and method implementing said device |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6843835B2 (en) | 2001-03-27 | 2005-01-18 | The Procter & Gamble Company | Air cleaning apparatus and method for cleaning air |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2684022A1 (en) * | 1991-11-22 | 1993-05-28 | Maulde Yan De | Device enabling air or a gas to be purified by scrubbing and conditioned |
JPH07119192A (en) * | 1993-10-22 | 1995-05-09 | Matsushita Electric Ind Co Ltd | Deodorization device |
WO1996020097A1 (en) | 1994-12-23 | 1996-07-04 | Alliedsignal Inc. | A filtration device using absorption for the removal of gas phase contaminants |
-
1997
- 1997-01-21 FR FR9700652A patent/FR2758612B1/en not_active Expired - Fee Related
-
1998
- 1998-01-16 AU AU59926/98A patent/AU5992698A/en not_active Abandoned
- 1998-01-16 WO PCT/FR1998/000076 patent/WO1998031970A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2684022A1 (en) * | 1991-11-22 | 1993-05-28 | Maulde Yan De | Device enabling air or a gas to be purified by scrubbing and conditioned |
JPH07119192A (en) * | 1993-10-22 | 1995-05-09 | Matsushita Electric Ind Co Ltd | Deodorization device |
WO1996020097A1 (en) | 1994-12-23 | 1996-07-04 | Alliedsignal Inc. | A filtration device using absorption for the removal of gas phase contaminants |
Non-Patent Citations (1)
Title |
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PATENT ABSTRACTS OF JAPAN vol. 095, no. 008 29 September 1995 (1995-09-29) * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20170010044A1 (en) * | 2013-12-11 | 2017-01-12 | Starklab | Device for producing a stream of air through a volume of liquid |
US11035614B2 (en) * | 2013-12-11 | 2021-06-15 | Starklab | Device for producing a stream of air through a volume of liquid |
US20170320006A1 (en) * | 2014-11-06 | 2017-11-09 | Starklab | Device for producing and treating a gas stream through a volume of liquid, and facility and method implementing said device |
US10946326B2 (en) * | 2014-11-06 | 2021-03-16 | Starklab | Device for producing and treating a gas stream through a volume of liquid, and facility and method implementing said device |
US11452965B2 (en) | 2014-11-06 | 2022-09-27 | Starklab | Device for producing and treating a gas stream through a volume of liquid, and facility and method implementing said device |
Also Published As
Publication number | Publication date |
---|---|
FR2758612B1 (en) | 1999-05-21 |
FR2758612A1 (en) | 1998-07-24 |
AU5992698A (en) | 1998-08-07 |
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