EP2668457B1 - Method and device for the heat treatment of wood using dust-free dehydrated gases - Google Patents
Method and device for the heat treatment of wood using dust-free dehydrated gases Download PDFInfo
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- EP2668457B1 EP2668457B1 EP12704876.7A EP12704876A EP2668457B1 EP 2668457 B1 EP2668457 B1 EP 2668457B1 EP 12704876 A EP12704876 A EP 12704876A EP 2668457 B1 EP2668457 B1 EP 2668457B1
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- gases
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- collection chamber
- fumes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D7/00—Forming, maintaining, or circulating atmospheres in heating chambers
- F27D7/06—Forming or maintaining special atmospheres or vacuum within heating chambers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/14—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects using gases or vapours other than air or steam, e.g. inert gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
- F26B25/006—Separating volatiles, e.g. recovering solvents from dryer exhaust gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
- F26B25/007—Dust filtering; Exhaust dust filters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/008—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases cleaning gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2210/00—Drying processes and machines for solid objects characterised by the specific requirements of the drying good
- F26B2210/16—Wood, e.g. lumber, timber
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Electrostatic Separation (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Treating Waste Gases (AREA)
Description
L'invention se rapporte à un procédé de traitement thermique du bois, dont le principe repose sur la génération de gaz chauds issus de la combustion de biomasse, lesdits gaz alimentant un four. Les traitements thermiques du bois permettent d'améliorer sa résistance biologique vis-à-vis des insectes et des champignons xylophages, ou encore d'accroître sa stabilité dimensionnelle grâce à une modification du matériau et sans l'introduction de produit chimique.The invention relates to a method of heat treatment of wood, the principle of which is based on the generation of hot gases from the combustion of biomass, said gases feeding an oven. Heat treatment of wood can improve its biological resistance to insects and xylophagous fungi, or increase its dimensional stability through a modification of the material and without the introduction of chemical.
Les procédés présents sur le marché, et qui permettent le traitement thermique du bois, utilisent l'électricité ou le gaz. Dans ce deuxième cas, les systèmes intervenant dans ces procédés, sont regroupés sous l'appellation de « générateurs d'air chauds », et fonctionnent sur le principe de l'air pulsé. Des ventilateurs permettent l'introduction de l'air servant à la combustion dans le foyer, les débits pouvant être modulés grâce à l'ajout d'un variateur. Les fumées issues du foyer sont aspirées au moyen d'un extracteur de fumées en sortie de cheminées, et passent à l'extérieur d'un échangeur de géométrie variable, pouvant par exemple être tubulaire ou carré. Ils transmettent alors leur chaleur à de l'air frais pulsé par un autre ventilateur dans l'échangeur. Le produit issu de ces générateurs d'air chaud, est donc un air à 20% d'oxygène, et dont la température n'excède généralement pas 150°C du fait de la forme de l'échangeur.Processes on the market, which allow the heat treatment of wood, use electricity or gas. In this second case, the systems involved in these processes, are grouped under the name of "hot air generators", and operate on the principle of forced air. Fans allow the introduction of air for combustion into the fireplace, the flow rates can be modulated through the addition of a dimmer. The flue gases from the furnace are sucked by means of a smoke extractor at the outlet of chimneys, and pass outside of a heat exchanger of variable geometry, which may for example be tubular or square. They then transmit their heat to fresh air pulsed by another fan in the exchanger. The product resulting from these hot air generators, is therefore an air with 20% oxygen, and whose temperature does not generally exceed 150 ° C because of the shape of the exchanger.
Les procédés de traitements thermiques à base de gaz issus de la combustion de biomasse, comme ils sont par exemple décrits dans la demande de brevet
Seulement, l'utilisation de la biomasse crée des contraintes supplémentaires liées à la production de fumées, fortement chargées en eau et en poussières, et qui doivent donc être traitées, sous peine d'engendrer une pollution notable de l'environnement, et sous peine de nuire éventuellement à la qualité du traitement thermique du bois.However, the use of biomass creates additional constraints related to the production of fumes, heavily loaded with water and dust, and must therefore be treated, otherwise it will cause significant pollution of the environment, otherwise the quality of the thermal treatment of wood could be affected.
Les procédés de traitement thermique du bois selon l'invention, et utilisant la biomasse pour la génération de gaz chauds, incluent non seulement une étape spécifique de déshydratation et de nettoyage des fumées, spécialement conçue pour permettre le nettoyage des fumées, afin de réaliser le traitement thermique du bois au moyen de gaz propres et non polluants, mais également des moyens additionnels pour piéger les particules polluantes résiduelles demeurant dans lesdites fumées. De cette manière, les procédés de traitement thermique du bois selon l'invention, mettent en oeuvre deux étapes de nettoyage pour accroitre la qualité des gaz en matière de propreté.The methods of heat treatment of the wood according to the invention, and using the biomass for the generation of hot gases, include not only a specific step of dehydration and flue cleaning, specially designed to allow the cleaning of fumes, to achieve the heat treatment of the wood with clean and non-polluting gases, but also additional means for trapping the residual pollutant particles remaining in said fumes. In this way, the wood heat treatment processes according to the invention, implement two cleaning steps to increase the quality of gas cleanliness.
L'invention a pour objet un procédé de traitement thermique du bois, comprenant dans l'ordre, une étape de production de gaz chauds et de fumées au moyen d'un générateur de gaz utilisant la biomasse, une étape de traitement des fumées consistant à déshydrater et à dépoussiérer les fumées par la mise en oeuvre de moyens spécifiques. une étape d'acheminement des gaz vers un four, une étape de chauffage du bois dans le four au moyen desdits gaz, et une étape d'extraction des vapeurs, , ladite étape de traitement des fumées s'effectuant au moyen d'un dispositif comprenant une chambre de refroidissement des gaz permettant de déshydrater lesdits gaz, ladite chambre de refroidissement étant prolongée par une première chambre de collecte des condensats issus de la déshydratation des fumées, ladite chambre de collecte étant située en dessous de la chambre de refroidissement, caractérisé en ce que la première chambre de collecte est surmontée par au moins un tube de sortie, dont le diamètre est dimensionné pour ralentir les gaz, et pour permettre la sédimentation des poussières. Autrement dit, le procédé de traitement thermique du bois selon l'invention, reposant sur la génération de gaz chauds au moyen d'une chaudière à biomasse, consacre une étape pleine et entière au nettoyage et à la déshydratation des fumées nocives issues du traitement thermique du bois. En effet, l'utilisation de la biomasse pour engendrer des gaz, entraine de façon quasiment systématique, l'émission de fumées fortement chargées en eau et en poussières, ayant pour conséquence, de polluer l'atmosphère et d'accroître les risques de nuire à la qualité du traitement thermique du bois. Or, habituellement, le traitement de ces vapeurs pouvait s'effectuer de façon indirecte et partielle, en jouant, par exemple, sur certains paramètres du procédé de traitement du bois, au risque de nuire à la qualité de ce traitement. En instaurant une étape spécifique de déshydratation et de dépoussiérage des fumées avec des moyens spécialement conçus pour remplir ces deux fonctions, les concepteurs du procédé de traitement thermique du bois selon l'invention, accordent une importance capitale à la réalisation du traitement thermique du bois au moyens de gaz réellement propres, pour un résultat optimisé et fiable, sans retombées néfastes sur l'environnement en termes de pollution. Le procédé selon l'invention, s'effectue en continu, au sein d'une installation isolée, sans perte de gaz, entre le générateur de gaz et l'extraction des vapeurs, et fonctionne à une pression basse. Ce procédé s'appuie également sur une étape finale d'extraction des vapeurs, au moyen par exemple de pompes, qui va influencer la géométrie, le dimensionnement et les caractéristiques fonctionnelles du dispositif, développé pour assurer cette phase de dépoussiérage et de déshydratation des fumées. Par la présence de tubes de sortie, les particules solides, qui se sont déposées sur la paroi interne de chacun desdits tubes de sortie, ont tendance à migrer par inertie vers la première chambre de collecte située en dessous. Cette première chambre de collecte sert à la fois de réceptacle pour les condensats issus de la chambre de refroidissement, et pour les particules solides qui se sont déposées dans chaque tube de sortie. De façon préférentielle, les gaz dans chaque tube de sortie sont ralentis de façon significative. Les condensats, qui se sont déposés sur les parois de la chambre de refroidissement, et qui migrent par inertie vers la première chambre de collecte, vont également servir à piéger les particules solides et les poussières des fumées, en les retenant à leur passage. La chambre de collecte possède ainsi une arrivée des gaz, en provenance de la chambre de refroidissement, ainsi qu'une sortie des gaz par l'intermédiaire de chacun des tubes de sortie.
vantageusement, l'étape de production des gaz au moyen du générateur de gaz est séparée de l'étape de traitement des fumées, par une étape de refroidissement, permettant de faire passer la température des gaz de 900°C à une température inférieure à 200°C. En effet, les opérations de déshydratation et de dépoussiérage des fumées, sont mieux maitrisées, et donc plus faciles à réaliser sur des gaz refroidis, plutôt que sur des gaz portés à des températures très élevées, voisines de 1000°C. Préférentiellement, les gaz sont refroidis à une température comprise entre 120°C et 200°C. Si cette étape de refroidissement est incluse dans le procédé de traitement thermique du bois selon l'invention, une étape de réchauffage des gaz refroidis devra être ajoutée dans ledit procédé, afin de réaliser l'étape de traitement thermique du bois dans le four avec des gaz suffisamment chauds.The subject of the invention is a method for heat treatment of wood, comprising in order a step of producing hot gases and fumes by means of a gas generator using biomass, a fume treatment stage consisting of dehydrate and dust off the fumes by the implementation of specific means. a step of conveying the gases to an oven, a step of heating the wood in the oven by means of said gases, and a step of extracting the vapors, said step of treating the fumes being effected by means of a device comprising a gas cooling chamber for dehydrating said gases, said cooling chamber being extended by a first condensate collection chamber resulting from the dehydration of the fumes, said collection chamber being located below the cooling chamber, characterized in that the first collection chamber is surmounted by at least one outlet tube, the diameter of which is sized to slow down the gases, and to allow the sedimentation of the dust. In other words, the method of heat treatment of the wood according to the invention, based on the generation of hot gases by means of a biomass boiler, devotes a full and complete step to the cleaning and dehydration of the harmful fumes resulting from the heat treatment. wood. Indeed, the use of biomass to generate gases, leads almost systematically, the emission of fumes heavily loaded with water and in dust, which has the effect of polluting the atmosphere and increasing the risks of adversely affecting the quality of the heat treatment of the wood. However, usually, the treatment of these vapors could be carried out indirectly and partially, by playing, for example, on certain parameters of the wood treatment process, at the risk of affecting the quality of this treatment. By instituting a specific step of dehydration and dedusting of fumes with means specially designed to fulfill these two functions, the designers of the wood heat treatment process according to the invention, attach great importance to the realization of heat treatment of wood at truly clean gas means, for an optimized and reliable result, without negative effects on the environment in terms of pollution. The method according to the invention is carried out continuously, in an isolated installation, without loss of gas, between the gas generator and the extraction of vapors, and operates at a low pressure. This process also relies on a final stage of extraction of the vapors, by means for example of pumps, which will influence the geometry, dimensioning and the functional characteristics of the device, developed to ensure this phase of dusting and dehydration of the fumes . By the presence of outlet tubes, the solid particles, which are deposited on the inner wall of each of said outlet tubes, tend to migrate by inertia to the first collection chamber located below. This first collection chamber serves both as a receptacle for condensates from the cooling chamber, and for solid particles that have deposited in each outlet tube. Preferably, the gases in each outlet tube are significantly slowed down. The condensates, which are deposited on the walls of the cooling chamber, and which migrate inertia to the first collection chamber, will also serve to trap the solid particles and dust fumes, retaining them in their passage. The collection chamber thus has a gas inlet from the cooling chamber and a gas outlet via each of the outlet tubes.
advantageously, the step of producing the gases by means of the gas generator is separated from the flue gas treatment step by a cooling step, making it possible to change the temperature of the gases from 900 ° C. to a temperature of less than 200 ° C. ° C. Indeed, dehydration and dust removal operations, are better controlled, and therefore easier to perform on cooled gases, rather than gas raised to very high temperatures, close to 1000 ° C. Preferentially, the gases are cooled to a temperature of between 120 ° C. and 200 ° C. If this cooling step is included in the method of heat treatment of the wood according to the invention, a step of reheating of the cooled gases will have to be added in said process, in order to carry out the step of heat treatment of the wood in the oven with sufficiently hot gases.
De façon préférentielle, l'étape de traitement des fumées s'effectue au moyen d'un dispositif comprenant une chambre de refroidissement des gaz, permettant de déshydrater lesdits gaz. En effet, puisque le procédé de traitement thermique du bois est basé sur l'aspiration des fumées, l'une des contraintes à respecter pour ledit procédé est de conserver une pression basse en tout point et à tout moment, dans l'installation prévue pour dérouler ce procédé de traitement du bois. Une augmentation de la perte de charge au passage des éléments de traitement des fumées, se traduit par une perte de débit d'aspiration et donc de puissance de la chaudière. De même, un fonctionnement en dépression et surpression élevée du système, signifie également une hausse de la consommation électrique qui pénalise le bilan énergétique du traitement. Pour toutes ces raisons, la déshydratation des fumées est donc réalisée par un refroidissement des fumées. De façon avantageuse, les fumées sont refroidies à 30°C dans cette chambre de refroidissement ou de déshydratation.Preferably, the fumes treatment step is performed by means of a device comprising a gas cooling chamber, for dehydrating said gases. Indeed, since the wood heat treatment process is based on the aspiration of the fumes, one of the constraints to be respected for said method is to keep a low pressure at any point and at any time, in the installation provided for unfold this wood treatment process. An increase in the pressure drop at the passage of the flue gas treatment elements, results in a loss of suction flow and thus power of the boiler. In the same way, a functioning in depression and high overpressure of the system, also means an increase of the electrical consumption which penalizes the energy balance of the treatment. For all these reasons, the dehydration of the fumes is therefore achieved by a cooling of the fumes. Advantageously, the fumes are cooled to 30 ° C in this cooling chamber or dehydration.
De façon avantageuse, la chambre de refroidissement est prolongée par une première chambre de collecte des condensats issus de la déshydratation des fumées, ladite chambre de collecte étant située en dessous de la chambre de refroidissement. En effet, les condensats qui se sont déposés sur les parois de la chambre de refroidissement, vont avoir tendance à ruisseler par inertie, le long de ces parois, pour se diriger vers la première chambre de collecte. Il est important de pouvoir concentrer ces condensats en un lieu bien spécifique et unique, ne risquant pas d'encrasser le dispositif de déshydratation et de dépoussiérage.Advantageously, the cooling chamber is extended by a first condensate collection chamber resulting from the dehydration of the fumes, said collection chamber being located below the cooling chamber. Indeed, the condensates that have been deposited on the walls of the cooling chamber, will tend to flow by inertia, along these walls, to go to the first collection chamber. It is important to be able to concentrate these condensates in a very specific and unique place, not risking to foul the device of dehydration and dedusting.
Préférentiellement, la première chambre de collecte est équipée de premiers moyens d'évacuation des condensats. En effet, une fois que les condensats se sont accumulés dans la première chambre de collecte, et afin de limiter les risques d'obturation totale ou partielle du circuit de circulation de gaz, il est souhaitable de pouvoir vider cette première chambre de collecte, au moyen d'une manipulation aisée et rapide, ne nécessitant pas l'interruption du procédé de traitement thermique du bois. Ces premiers moyens d'évacuation peuvent être activés manuellement, ou se déclencher automatiquement une fois un taux seuil de remplissage atteint dans la chambre de collecte. Ces premiers moyens d'évacuation pourraient également se déclencher automatiquement par cycle de temps préprogrammés.Preferably, the first collection chamber is equipped with first condensate discharge means. Indeed, once the condensates have accumulated in the first collection chamber, and to limit the risk of total or partial closure of the gas circulation circuit, it is desirable to be able to empty this first collection chamber, at easy and fast handling, not requiring the interruption of the wood heat treatment process. These first evacuation means can be activated manually, or trigger automatically once a threshold filling rate reached in the collection chamber. These first evacuation means could also be triggered automatically by preprogrammed time cycle.
De façon préférentielle, chaque tube de sortie est muni d'au moins un filtre électrostatique destiné à fixer les poussières. Ces filtres sont disposés de façon transversale dans chaque tube, et ont pour but de retenir toutes les particules solides ou les poussières transportées par les gaz passant dans lesdits tubes. Lesdites particules ou poussières s'agglutinent contre la face inférieure de chaque filtre, et ont tendance à tomber dans la première chambre de collecte. Ces filtres permettent la fixation des poussières sur chaque tube de sortie, pour une perte de charge quasiment nulle.Preferably, each outlet tube is provided with at least one electrostatic filter for fixing the dust. These filters are arranged transversely in each tube, and are intended to retain any solid particles or dust transported by the gas passing through said tubes. Said particles or dust agglutinate against the underside of each filter, and tend to fall into the first collection chamber. These filters allow the fixing of dust on each outlet tube, for a loss of almost zero load.
De façon avantageuse, la première chambre de collecte est équipée de deuxièmes moyens d'évacuation des particules solides. En effet, pour les mêmes raisons que celles invoquées pour les condensats, il est souhaitable de pouvoir débarrasser la première chambre de collecte, des particules solides ou poussières qui se sont accumulées dans celle-ci, sans avoir à interrompre le procédé de traitement selon l'invention. Ces deuxièmes moyens d'évacuation peuvent être activés manuellement, ou se déclencher automatiquement une fois un taux seuil de remplissage atteint dans la chambre de collecte. Ils pourraient également se déclencher automatiquement par cycle de temps préprogrammés. De façon préférentielle, chaque tube de sortie de la première chambre de collecte, débouche dans une deuxième chambre de collecte située au dessus de la première chambre de collecte, et dotée d'une tubulure de sortie reliée à un système d'aspiration des gaz. Ces moyens d'aspiration permettent d'assurer la circulation continue des gaz dans le dispositif de traitement.Advantageously, the first collection chamber is equipped with second means for discharging the solid particles. Indeed, for the same reasons as those invoked for condensates, it is desirable to be able to rid the first collection chamber, solid particles or dust that have accumulated in it, without having to interrupt the treatment method according to the invention. These second evacuation means can be activated manually, or trigger automatically once a threshold filling rate reached in the collection chamber. They could also be triggered automatically by preprogrammed time cycle. Preferably, each outlet tube of the first collection chamber, opens into a second collection chamber located above the first collection chamber, and provided with an outlet pipe connected to a gas suction system. These suction means make it possible to ensure the continuous circulation of the gases in the treatment device.
Avantageusement, chaque tube de sortie (20,21) a un diamètre supérieur ou égal à 200mm.Advantageously, each outlet tube (20,21) has a diameter greater than or equal to 200 mm.
Préférentiellement, chaque tube de sortie (20,21) est dimensionné pour faire chuter la vitesse des gaz à une valeur inférieure ou égale à 3m/s.Preferably, each outlet tube (20,21) is dimensioned to reduce the speed of the gas to a value less than or equal to 3m / s.
L'invention se rapporte également à un dispositif pour réaliser l'étape de traitement des fumées d'un procédé selon l'invention. La principale caractéristique d'un dispositif selon l'invention est qu'il comprend une chambre de refroidissement présentant un orifice pour l'arrivée des gaz issus du générateur de gaz, ladite chambre de refroidissement débouchant dans une première chambre de collecte, équipée de premiers moyens d'évacuation des condensats et de deuxièmes moyens d'évacuation des particules solides, ladite première chambre étant prolongée par deux tubes de sortie débouchant dans une deuxième chambre de collecte dotée d'une tubulure de sortie reliée à un système d'aspiration, le diamètre desdits tubes étant dimensionné pour réduire la vitesse des gaz.The invention also relates to a device for carrying out the fumes treatment step of a method according to the invention. The main characteristic of a device according to the invention is that it comprises a cooling chamber having an orifice for the arrival of the gases from the gas generator, said cooling chamber opening into a first collection chamber, equipped with first means for discharging the condensates and second means for discharging the solid particles, said first chamber being extended by two outlet tubes opening into a second collection chamber provided with an outlet pipe connected to a suction system; diameter of said tubes being dimensioned to reduce the speed of the gases.
Avantageusement, la chambre de refroidissement est verticale, et les deux chambres de collecte sont horizontales, la deuxième chambre étant située au dessus de la première chambre, et les deux tubes de sortie reliant lesdites chambres de collecte, sont verticaux et sont chacun dotés d'un filtre électrostatique de retenue des poussières.Advantageously, the cooling chamber is vertical, and the two collection chambers are horizontal, the second chamber being located above the first chamber, and the two outlet tubes connecting said collection chambers, are vertical and are each provided with an electrostatic dust filter.
Préférentiellement, le dispositif constitue un circuit de gaz isolé, ayant un orifice d'entrée des gaz chauds, et un orifice de sortie des gaz traités. De cette manière il peut venir s'insérer facilement, dans un conduit de gaz chauds, destiné à alimenter un four de traitement thermique du bois.Preferably, the device constitutes an insulated gas circuit, having a hot gas inlet orifice, and a treated gas outlet orifice. In this way it can be inserted easily, in a hot gas duct, for supplying a wood heat treatment furnace.
Les procédés de traitement selon l'invention, présentent l'avantage de mettre en oeuvre une étape de déshydratation et de dépoussiérage des fumées au moyen d'un dispositif compact, peu encombrant et performant. De plus, le dispositif est conçu pour réaliser ces deux opérations de façon quasi-simultanée, permettant un gain de temps au niveau du procédé de traitement selon l'invention. Enfin, le dispositif de traitement a l'avantage d'être doté de systèmes d'évacuation des condensats et/ou des particules solides récupérés des fumées, évitant un encrassement total ou partiel, pouvant conduire à une interruption du procédé de traitement selon l'invention.The treatment processes according to the invention have the advantage of implementing a step of dehydration and dedusting fumes by means of a compact device, compact and efficient. In addition, the device is designed to perform these two operations almost simultaneously, allowing time savings in the treatment method according to the invention. Finally, the treatment device has the advantage of being equipped with condensate removal systems and / or solid particles recovered from the fumes, avoiding total or partial fouling, which can lead to an interruption of the treatment process according to the invention. invention.
On donne ci-après une description détaillée d'un mode de réalisation préféré d'un procédé de traitement thermique du bois selon l'invention, ainsi que d'un dispositif de traitement des fumées selon l'invention, en se référant aux
- La
figure 1 est une vue schématisée des différents blocs matérialisant les différentes étapes d'un procédé de traitement selon l'invention, - La
figure 2 , est une vue en perspective d'un dispositif de traitement des fumées selon l'invention.
- The
figure 1 is a schematic view of the different blocks embodying the different steps of a treatment method according to the invention, - The
figure 2 , is a perspective view of a smoke treatment device according to the invention.
En se référant à la
En se référant à la
Le mode de fonctionnement de ce dispositif de traitement 10 est le suivant. Les gaz chauds issus du générateur de gaz utilisant la biomasse, sont émis à 900°C environ, puis sont refroidis à une température comprise entre 120°C et 200°C, au moyen d'un échangeur de refroidissement placé en amont du dispositif de traitement 10. La notion d' « amont » est à considérer par rapport au sens de propagation des gaz. Les gaz refroidis, mais demeurant toujours chauds par rapport à la température ambiante, pénètrent dans le dispositif de traitement 10 par l'orifice d'entrée 13. Ils traversent d'abord la chambre de refroidissement 15, où ils sont refroidis jusqu'à une température de l'ordre de 30°C, et sont donc déshydratés, les condensats se déposant sur la paroi 19 de cette chambre 15. Les gaz refroidis arrivent ensuite dans la première chambre de collecte 17. Sous l'effet de la pression, ils remontent vers la deuxième chambre de collecte 23, en empruntant les deux tubes de sortie 20,21, dont le diamètre important va réduire leur vitesse de progression à 3m/s. Ils traversent alors les filtres électrostatiques 26,27, qui piègent leurs poussières. Les gaz propres et refroidis à environ 40°C, arrivent dans la deuxième chambre 23 de collecte supérieure, où ils sont alors acheminés, via la tubulure de sortie 30, vers un système d'aspiration. Les condensats déposés sur la paroi 19 de la chambre de refroidissement 15, et les poussières piégées par les deux filtres électrostatiques 26,27, migrent vers la première chambre de collecte 17, d'où ils peuvent être évacués avec les moyens 28,29 appropriés.The operating mode of this
Claims (9)
- A method for the heat treatment of wood, comprising, in order:- a step for producing (1) hot gases and fumes using a gas generator using biomass,- a step for treating (3) fumes consisting of dehydrating and removing dust from the fumes by implementing specific means (10), said step being carried out using a device (10) comprising a cooling chamber (15) for the gases making it possible to dehydrate said gases, said cooling chamber (15) being extended by a first collection chamber (17) for condensates derived from the dehydration of the fumes, said collection chamber (17) being situated below the cooling chamber (15) and being topped by at least one outlet tube (20, 21), the diameter of which is dimensioned to slow the gases, and to allow the sedimentation of the dusts,- a step for conveying (40) gases toward a furnace,- a step for heating (5) wood in the furnace using said gases,- a step for extraction (6) of the vapors,characterized in that each outlet tube (20, 21) has a diameter larger than or equal to 200 mm so as to cause the speed of the gases to drop to a value below or equal to 3 m/s.
- The method according to claim 1, characterized in that the step for producing (1) gases using the gas generator is separated from the step for treating (3) fumes, by a cooling step (2) making it possible to bring the temperature of the gases from 900°C to a temperature below 200°C.
- The method according to claim 1, characterized in that the first collection chamber (17) is equipped with first means (28) for evacuating condensates.
- The method according to claim 1, characterized in that each outlet tube (20, 21) is provided with at least one electrostatic filter (26, 27) intended to catch dust.
- The method according to any one of claims 1 to 4, characterized in that the first collection chamber (17) is equipped with second means (29) for evacuating solid particles.
- The method according to any one of claims 1 or 4, characterized in that each outlet tube (20, 21) of the first collection chamber (17) emerges in a second collection chamber (23) situated above the first collection chamber (17), and provided with an outlet tubing (30) connected to a gas suction system.
- A device (10) for carrying out the step for treating fumes of a method according to any one of claims 1 to 6, comprising a cooling chamber (15) having an orifice (13) for the arrival of gases derived from the gas generator, said cooling chamber (15) emerging in a first collection chamber (17), equipped with first means (28) for discharging condensates and second means (29) for discharging solid particles, said first chamber (17) being extended by two outlet tubes (20, 21) emerging in a second collection chamber (23) provided with an outlet tubing (30) connected to a suction system, characterized in that each outlet tube (20, 21) has a diameter larger than or equal to 200 mm so as to cause the speed of the gases to drop to a value below or equal to 3 m/s.
- The device according to claim 7, characterized in that the cooling chamber (15) is vertical, and the two collection chambers (17, 23) are horizontal, the second chamber (23) being situated above the first chamber (17), and in that the two outlet tubes (20, 21) connecting said collection chambers (17, 23) are vertical and are each provided with an electrostatic filter (26, 27) for dust retention.
- The device according to any one of claims 7 or 8, characterized in that it constitutes an isolated gas circuit, having a hot gas inlet orifice (13), and a treated gas outlet orifice (30).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1150559A FR2970772B1 (en) | 2011-01-25 | 2011-01-25 | PROCESS FOR THE THERMAL TREATMENT OF WOOD WITH GASES DEHYDRATES AND DEOUSSIERS |
PCT/FR2012/050110 WO2012101359A1 (en) | 2011-01-25 | 2012-01-19 | Method for the heat treatment of wood using dust-free dehydrated gases |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2668457A1 EP2668457A1 (en) | 2013-12-04 |
EP2668457B1 true EP2668457B1 (en) | 2018-03-07 |
Family
ID=45688895
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP12704876.7A Not-in-force EP2668457B1 (en) | 2011-01-25 | 2012-01-19 | Method and device for the heat treatment of wood using dust-free dehydrated gases |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP2668457B1 (en) |
FR (1) | FR2970772B1 (en) |
WO (1) | WO2012101359A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104110969B (en) | 2014-07-11 | 2016-03-30 | 深圳市华星光电技术有限公司 | A kind of gas cooling device and high-temperature operation system |
CN104501570B (en) * | 2014-12-17 | 2017-01-04 | 福建省永安林业(集团)股份有限公司 | A kind of dry kiln device |
CN104501547B (en) * | 2014-12-17 | 2017-01-04 | 福建省永安林业(集团)股份有限公司 | A kind of dry kiln system of radiator, furnace gas mixing application |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2870154B1 (en) * | 2004-05-13 | 2012-12-14 | Bio 3D Applic | BIO-THERMAL METHOD AND SYSTEM FOR STABILIZING LUMBER |
FR2902866B1 (en) | 2006-06-22 | 2008-10-10 | Giat Ind Sa | HOT GAS GENERATOR AND DRYING OR DEHYDRATION INSTALLATION USING SUCH A GENERATOR |
FR2907884B1 (en) * | 2006-10-25 | 2012-12-21 | Giat Ind Sa | METHOD FOR THERMALLY TREATING A MATERIAL, IN PARTICULAR WOOD, AND THERMAL TREATMENT UNIT USING SUCH A METHOD |
-
2011
- 2011-01-25 FR FR1150559A patent/FR2970772B1/en not_active Expired - Fee Related
-
2012
- 2012-01-19 EP EP12704876.7A patent/EP2668457B1/en not_active Not-in-force
- 2012-01-19 WO PCT/FR2012/050110 patent/WO2012101359A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
FR2970772B1 (en) | 2017-06-23 |
EP2668457A1 (en) | 2013-12-04 |
WO2012101359A1 (en) | 2012-08-02 |
FR2970772A1 (en) | 2012-07-27 |
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