EP0795594B1 - Plant for the environmentally friendly thermal treatment of industrial, hospital, domestic and the like waste - Google Patents
Plant for the environmentally friendly thermal treatment of industrial, hospital, domestic and the like waste Download PDFInfo
- Publication number
- EP0795594B1 EP0795594B1 EP19970400483 EP97400483A EP0795594B1 EP 0795594 B1 EP0795594 B1 EP 0795594B1 EP 19970400483 EP19970400483 EP 19970400483 EP 97400483 A EP97400483 A EP 97400483A EP 0795594 B1 EP0795594 B1 EP 0795594B1
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- Prior art keywords
- furnace
- distillation
- cell
- gas
- sealed
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B7/00—Coke ovens with mechanical conveying means for the raw material inside the oven
- C10B7/14—Coke ovens with mechanical conveying means for the raw material inside the oven with trucks, containers, or trays
Definitions
- the present invention relates to an installation implementing a process for heat treatment of industrial and hospital waste, household and similar, at low temperature and under partial vacuum, whether are in solid, liquid or gaseous form.
- the products are distilled by heat treatment, at 500 ° C and partial vacuum (100 mb). This process accelerates decomposition organic matter by facilitating molecular bursting and avoids default oxygen self-combustion.
- the added or substituted atoms, in ionized (gaseous) form, are treated by neutralization. At the end decomposition of organic products, due to heat treatment, the products are transformed into gas, hydrocarbons, coal.
- the installation is composed of the assemblies as defined in the wording of the dependent claim.
- the products to be treated are deposited, without prior sorting or packaging in a collection bucket (1/1) which is introduced into an enclosure distillation (2/1). This is closed hermetically, then purged of its atmosphere by a pumping group (9/1), the heating (board 2/3) is then put into service for a free rise up to 150 ° C. This temperature will be maintained for 30 minutes which constitutes the dehydration level and vaporization of certain products. At the end of this stage, the rise temperature is resumed up to 500 ° C, at this level it is maintained during one hour. At the end of this period the oven (3/1) is moved to put the speaker in the open air and thereby accelerate its cooling which can be improved by precipitation of water.
- the gases are sucked in by a group pumping (9/1) through a condenser (7/1) and discharged into a washing column (10/1) to remove halogens. They are taken back and tablets for storage for later use.
- aqueous phase of the washing column and the condensates are adjusted in "pH" and precipitated in a settling tank (15/1) to recover the hydrocarbons in suspension, then filtered. After analysis, the waters are either reused by the installation itself or discharged into the sewer (22/1) for the rest.
- the collecting bucket (1/1) is then extracted from the enclosure (2/1) and placed on a rocker which will pour its solid stream onto a conveyor (23/1).
- the solids will be sorted for recovery or landfill without harm to the environment.
- the installation according to the invention implements the equipment described hereinafter.
- Heat treatment equipment that includes collection bins (1/1), two sealed distillation chambers (2/1) and the oven itself says (3/1).
- the collection bins (1/1) are bins made of stainless steel sheet can be mounted on engineered pads allowing their grip by an elevating machine, or on cast iron wheels for a manual handling when the mass of the products to be treated is low.
- the blanks of the bins are equipped with an axis of rotation for their tilting during unloading.
- the bins receive directly, without sorting or handling human, therefore without risk for the operator, the products to be treated.
- the distillation chambers (2/2) are parallelepiped boxes stainless steel closed at one end by a watertight door fitted with a metal structure seal.
- the door pivots on an axis to come and run parallel to the facade of the enclosure on which it is pressed by a system with cleats and wedges biased.
- the pregnant are located face to face, separated from each other by a loading table. They rest on cradles placed on the floor of the oven. Inside, andirons in the form of raceways, rails or trays, receive the collection bucket.
- a stainless steel tube opening at a low point in the enclosure will connect it to the extraction system distillation gases. During precipitation cooling water will be collected in a receptacle located under the enclosure.
- the oven (3/1) consists of a casing, of welded construction, in trade sheet and profiles. It circulates on rails, of an enclosure to the other, by means of two motorized rollers and free rollers. It is closed at both ends by so-called "guillotine" doors operated by winches. The high position of the doors allows the movement of the oven. In the low position the doors are pressed on the facades by a cylinder system. Plating the doors authorizes heating. The casing and the doors are thermally insulated by a lining of ceramic fibers. The electric heating of the oven is ensured by resistant elements, formed in waves, in Nickel / Chromium alloy. A turbine recirculation will ensure forced convection of ambient air.
- the power supply of the heating elements, the turbine and the operating devices are made by a bundle of festoon-mounted cables to follow the movements of the oven.
- the heating regulator is a thyristor power unit.
- the two oven bases are bases made of refractory concrete placed directly on the floor of the room.
- the distillation gas treatment system contains the main elements described below.
- the condenser (7/1) has two functions: trapping condensable gases and cool the incondensable gases before their aspiration.
- the device consists of a waterproof stainless steel container in which plates are arranged in baffles. These plates, presenting a large heat exchange surface, are kept at low temperature by circulation of water, previously chilled (14/1), in coils soldered on.
- the pumping group (9/1) consists of a rotary piston pump without lubrication and a menbran pump. Upstream of the group is installed a particle filter (8/1).
- the washing column (10/1) is in the form of a sealed silo stainless steel in which a constant water level is maintained.
- the gases discharged by the pumping unit are conveyed in a sheath, comprising a washing ramp forming a film of water, which dives below the level of the water table. The gases are therefore washed by precipitation and bubbling.
- Solenoid valves allow the automation of the operation of the installation from information given by measuring, control and analysis.
- the water requirements of the installations are as follows: cooling water condenser plates, level maintenance in the washing column, the water precipitated on the distillation chamber to be cooled, the water from washing of premises and equipment. By cons we recover some amount of water after condensation of the vapors from the enclosure distillation.
- the liquids to be treated come from the condenser, the gas washing column, collection of premises clean water and materials.
- the condenser cooling water is clean and to the advantage to be refreshed.
- the enclosure cooling water is also clean but can be loaded with dust, it will be filtered (17/1) before being switched back on.
- the essential components water treatment system are: the tank intended to preserve the correct amount of water (13/1), the appliance for cooling the plates condenser (14/1), the washing column (10/1), the drain pan decanting of hydrocarbons (15/1), the oil storage tank (16/1), the system driven by the results of the addition analyzes of washing liquid to the waters to be neutralized.
- This system is classic to water chemistry and is not the subject of a particular description.
- the residual solid elements are discharged onto a conveyor (23/1), on the other hand, for coals, sucked up (24/1) and put in silo (25/1). Heavy materials returned clean are sent to sorting (26-27-28-29 / 1) classic for the recovery industries.
- the operating measures which trigger the different phases of the security measures to protect the equipment and therefore personnel
- the quality measures to guarantee and demonstrate respect for the environment
- profitability measures installation there are four types of measurements to be made: the operating measures which trigger the different phases of the security measures to protect the equipment and therefore personnel
- the quality measures to guarantee and demonstrate respect for the environment
- profitability measures installation there are four types of measurements to be made: the operating measures which trigger the different phases of the security measures to protect the equipment and therefore personnel, the quality measures to guarantee and demonstrate respect for the environment, profitability measures installation.
- the measurements are carried out by probes or sensors which are associated to monitoring or control apparatus.
- certain measures deemed essential are archived in graphic form or in alphanumeric messages. This archiving ensures maintenance assistance of materials and the conservation of the treatment history. Management of the entire installation is entrusted to a programmable controller, real-time or delayed measurement monitoring is ensured by a system computerized visualization.
- the operating measurements relate to: the internal temperature of the distillation chamber which is taken into account by a regulator / programmer which itself controls the power unit to thyristors, the value of the depression in the enclosure that triggers the start-up of the heating system, the flow of aspirated gases, the temperature upstream of the pumping unit, the level of liquids collected at the base of the condenser, the level in the washing column, the rate of filling tanks.
- the safety measures concern: the temperature of the heating elements of the oven to avoid overheating detrimental to the performance of the equipment over time, the internal pressures of the condenser and the washing, the gas flow rates at the inlet and outlet of the condenser, the refrigeration temperature of the condenser plates.
- Quality measures concern analysis of noncondensable gases, analysis of recycled water, analysis of the local atmosphere, temperature and flow of water to be discharged to the sewer.
- the profitability measures concern the weight of the products to be treated, consumption of electrical energy and consumption of city water. These measures will make it possible to establish an operating balance sheet.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
La présente invention concerne une installation mettant en oeuvre un procédé de traitement thermique de déchets industriels, hospitaliers, ménagers et assimilables, à basse température et sous vide partiel, qu'ils soient sous forme solide, liquide ou gazeuse.The present invention relates to an installation implementing a process for heat treatment of industrial and hospital waste, household and similar, at low temperature and under partial vacuum, whether are in solid, liquid or gaseous form.
Les techniques actuellement employées nécessitent soit un tri préalable des produits qui implique des risques pour le personnel, soit un conditionnement spécifique, soit un transfert, donc une manoeuvre, en cours de traitement. En outre, dans un procédé en vase clos, même à basse température, le temps de cycle est prolongé très sensiblement par la phase de refroidissement de la matière secondaire solide ce qui pénalise d'autant la rentabilité de l'installation. D'autre part, les gaz issus du traitement doivent être aspirés par un groupe de pompage et pour cela préalablement refroidis. Les matériels implantés en amont de la pompe à vide peuvent se colmater ou, si on utilise la technique du barbotage des gaz dans de l'eau, celle-ci est portée à une température excessive qui la rend impropre à son rejet sans un nouveau traitement. Dans le cas ou les produits sont traités par incinération, c'est à dire à haute température, les produits gazeux sont évacués dans l'atmosphère ce qui ne donne pas toute garantie quant à la protection de l'environnement. Le brevet européen EP-A-0505278 décrit un système, pour le traitement par thermolyse de produits solides dont le rejet est préjudiciable pour l'environnement.The techniques currently used require either a preliminary sorting products that involve risks for personnel, i.e. specific conditioning, i.e. a transfer, therefore a maneuver, in course of treatment. In addition, in a closed process, even at low temperature, the cycle time is very significantly extended by the phase cooling of the solid secondary material which penalizes all the more the profitability of the installation. On the other hand, the gases from the treatment must be vacuumed by a pumping unit and for this beforehand cooled. The equipment installed upstream of the vacuum pump can clogging or, if the gas bubbling technique is used in water, it is brought to an excessive temperature which makes it unsuitable to its rejection without further treatment. In case the products are treated by incineration, i.e. at high temperature, the products gases are discharged into the atmosphere which does not give any guarantee in terms of environmental protection. European patent EP-A-0505278 describes a system for the thermolysis treatment of solid products of which the release is harmful to the environment.
Le système faisant l'objet de la présente invention prétend remédier à ces inconvénients.The system which is the subject of the present invention claims to remedy to these disadvantages.
La distillation des produits s'effectue par traitement thermique, à 500°C et sous vide partiel (100 mb). Ce procédé accélère la décomposition des matières organiques en facilitant l'éclatement moléculaire et évite l'autocombustion par défaut d'oxygène. Les atomes ajoutés ou substitués, sous forme ionisée (gazeuse), sont traités par neutralisation. Au terme de la décomposition des produits organiques, dû au traitement thermique, les produits sont transformés en gaz, hydrocarbures, charbon.The products are distilled by heat treatment, at 500 ° C and partial vacuum (100 mb). This process accelerates decomposition organic matter by facilitating molecular bursting and avoids default oxygen self-combustion. The added or substituted atoms, in ionized (gaseous) form, are treated by neutralization. At the end decomposition of organic products, due to heat treatment, the products are transformed into gas, hydrocarbons, coal.
L'installation, selon la présente invention, est composée des ensembles tel que défini dans le libellé de la revendication dépendente.The installation, according to the present invention, is composed of the assemblies as defined in the wording of the dependent claim.
Les revendications dépendentes 2 et 3 contiennent des réalisations particulières de l'invention. Dependent claims 2 and 3 contain embodiments particular features of the invention.
Les produits à traiter sont déposés, sans tri ni conditionnement préalables
dans une benne de collecte (1/1) qui est introduite dans une enceinte
de distillation (2/1). Celle-ci est fermée hermétiquement, puis purgée
de son atmosphère par un groupe de pompage (9/1), le chauffage (planche
2/3) est alors mis en service pour une montée libre jusqu'à 150°C. Cette
température sera maintenue 30 mn ce qui constitue le palier de déshydratation
et de vaporisation de certains produits. Au terme de ce palier, la montée
en température est reprise jusqu'à 500°C, à ce niveau elle est maintenue
pendant une heure. A la fin de cette période le four (3/1) est déplacé
pour mettre l'enceinte à l'air libre et par là même accélérer son
refroidissement celui-ci pouvant être amélioré par précipitation d'eau.
Pendant le cycle thermique (planche 2/3) les gaz sont aspirés par un groupe
de pompage (9/1) au travers d'un condenseur (7/1) et refoulés dans une
colonne de lavage (10/1) afin d'éliminer les halogènes. Ils sont repris
et comprimés pour stockage en vue d'une utilisation ultérieure.The products to be treated are deposited, without prior sorting or packaging
in a collection bucket (1/1) which is introduced into an enclosure
distillation (2/1). This is closed hermetically, then purged
of its atmosphere by a pumping group (9/1), the heating (
La phase acqueuse de la colonne de lavage et les condensats sont ajustés en "pH" et précipités dans un bac de décantation (15/1) pour récupérer les hydrocarbures en suspension, puis filtrés. Après analyse, les eaux sont soit réutilisées par l'installation elle-même, soit rejetées à l'égout (22/1) pour le surplus.The aqueous phase of the washing column and the condensates are adjusted in "pH" and precipitated in a settling tank (15/1) to recover the hydrocarbons in suspension, then filtered. After analysis, the waters are either reused by the installation itself or discharged into the sewer (22/1) for the rest.
Après dégagement du four mobile (3/1), dès que la température de l'enceinte de distillation (2/1) est redescendue à une valeur inférieure à 80°C un signal avertit l'exploitant de l'installation de la fin du traitement et de la possibilité de déchargement.After release of the mobile oven (3/1), as soon as the temperature of the enclosure distillation (2/1) is lowered to a value below 80 ° C a signal warns the plant operator of the end of treatment and the possibility of unloading.
La benne de collecte (1/1) est alors extraite de l'enceinte (2/1) et placée sur un basculeur qui déversera son continu solide sur un convoyeur (23/1). Les solides seront triés en vue de leur récupération ou de leur mise en décharge sans nuisance pour l'environnement.The collecting bucket (1/1) is then extracted from the enclosure (2/1) and placed on a rocker which will pour its solid stream onto a conveyor (23/1). The solids will be sorted for recovery or landfill without harm to the environment.
L'installation, selon l'invention, met en oeuvre le matériel décrit ci-aprés.The installation according to the invention implements the equipment described hereinafter.
Un équipement de traitement thermique qui comprend des bennes de collecte (1/1), deux enceintes étanches de distillation (2/1) et le four proprement dit (3/1).Heat treatment equipment that includes collection bins (1/1), two sealed distillation chambers (2/1) and the oven itself says (3/1).
Le four est de type "voute roulante" (voir planche 3/3) dont la mobilité représente les avantages suivants:
- accélération du refroidissement des produits traités par mise à l'air libre de l'enceinte de distillation et précipitation d'eau,
- possibilité de mettre en chauffe une enceinte pendant le refroidissement de l'autre et ainsi augmenter le rendement du matériel.
- acceleration of the cooling of the treated products by venting the distillation chamber and precipitation of water,
- possibility of heating one enclosure during the cooling of the other and thus increasing the efficiency of the equipment.
Les bennes de collecte (1/1) sont des bacs en tôle d'acier inoxydable pouvant être montés sur des patins ouvragés permettant leur préhension par un engin élévateur, ou sur des roues en fonte réfractaire pour une manutention manuelle lorsque la masse des produits à traiter est faible. Les flans des bacs sont équipés d'axe de rotation pour leur basculement lors du déchargement. Les bacs reçoivent directement, sans tri ni manipulation humaine, donc sans risque pour l'exploitant, les produits à traiter.The collection bins (1/1) are bins made of stainless steel sheet can be mounted on engineered pads allowing their grip by an elevating machine, or on cast iron wheels for a manual handling when the mass of the products to be treated is low. The blanks of the bins are equipped with an axis of rotation for their tilting during unloading. The bins receive directly, without sorting or handling human, therefore without risk for the operator, the products to be treated.
Les enceintes de distillation (2/2) sont des caissons parallélépipèdes en acier inoxydable fermés à l'une de leur extrémité par une porte étanche équipée d'un joint à structure métallique. La porte pivote sur un axe pour venir se présenter parallèlement à la façade de l'enceinte sur laquelle elle est plaquée par un système à taquets et cales biaises. Les enceintes sont implantées face à face, séparées entre elle par une table de chargement. Elles reposent sur des berceaux placés sur les soles du four. A l'intérieur, des chenets sous forme de chemins de roulement, de rails ou de plateaux, reçoivent la benne de collecte. Une tubulure en acier inoxydable débouchant en point bas dans l'enceinte reliera celle-ci au système d'extraction des gaz de distillation. Lors du refroidissement par précipitation l'eau sera recueillie dans un réceptacle situé sous l'enceinte.The distillation chambers (2/2) are parallelepiped boxes stainless steel closed at one end by a watertight door fitted with a metal structure seal. The door pivots on an axis to come and run parallel to the facade of the enclosure on which it is pressed by a system with cleats and wedges biased. The pregnant are located face to face, separated from each other by a loading table. They rest on cradles placed on the floor of the oven. Inside, andirons in the form of raceways, rails or trays, receive the collection bucket. A stainless steel tube opening at a low point in the enclosure will connect it to the extraction system distillation gases. During precipitation cooling water will be collected in a receptacle located under the enclosure.
Le four (3/1) est constitué d'un casing, de construction soudée, en tôle et profilés du commerce. Il circule sur des rails, d'une enceinte à l'autre, au moyen de deux galets motorisés et de galets libres. Il est fermé en ses deux extrémités par des portes dites "à guillotine" manoeuvrées par des treuils. La position haute des portes permet le déplacement du four. En position basse les portes sont plaquées sur les façades par un système à vérins. Le plaquage des portes autorise la mise en chauffe. Le casing et les portes sont isolés thermiquement par un garnissage de fibres céramiques. Le chauffage électrique du four est assuré par des éléments résistants, formés en ondes, en alliage Nickel/Chrome. Une turbine de recirculation assurera la convection forcée de l'air ambiant. L'alimentation électrique des éléments chauffants, de la turbine et des organes de manoeuvre se fait par un faisceau de câbles montés en feston pour suivre les mouvements du four. L'organe réglant du chauffage est une unité de puissance à thyristors. Les deux soles du four sont des embases en béton réfractaire placées directement sur le sol du local.The oven (3/1) consists of a casing, of welded construction, in trade sheet and profiles. It circulates on rails, of an enclosure to the other, by means of two motorized rollers and free rollers. It is closed at both ends by so-called "guillotine" doors operated by winches. The high position of the doors allows the movement of the oven. In the low position the doors are pressed on the facades by a cylinder system. Plating the doors authorizes heating. The casing and the doors are thermally insulated by a lining of ceramic fibers. The electric heating of the oven is ensured by resistant elements, formed in waves, in Nickel / Chromium alloy. A turbine recirculation will ensure forced convection of ambient air. The power supply of the heating elements, the turbine and the operating devices are made by a bundle of festoon-mounted cables to follow the movements of the oven. The heating regulator is a thyristor power unit. The two oven bases are bases made of refractory concrete placed directly on the floor of the room.
Selon l'invention, le système de traitement des gaz de distillation comporte les principaux éléments décrits ci-après.According to the invention, the distillation gas treatment system contains the main elements described below.
Le condenseur (7/1) a deux fonctions: pièger les gaz condensables et refroidir les gaz incondensables avant leur aspiration. The condenser (7/1) has two functions: trapping condensable gases and cool the incondensable gases before their aspiration.
L'appareil est constitué d'un récipient étanche en acier inoxydable dans lequel sont disposées des plaques en chicanes. Ces plaques, présentant une grande surface d'échange thermique, sont maintenues à basse température par circulation d'eau, préalablement réfrigérée (14/1), dans des serpentins soudés dessus.The device consists of a waterproof stainless steel container in which plates are arranged in baffles. These plates, presenting a large heat exchange surface, are kept at low temperature by circulation of water, previously chilled (14/1), in coils soldered on.
Le groupe de pompage (9/1) se compose d'une pompe à pistons rotatifs sans lubrification et d'une pompe à menbrane. En amont du groupe est installé un filtre à particules (8/1).The pumping group (9/1) consists of a rotary piston pump without lubrication and a menbran pump. Upstream of the group is installed a particle filter (8/1).
La colonne de lavage (10/1) se présente sous la forme d'un silo étanche en acier inoxidable dans lequel on maintient un niveau d'eau constant. Selon l'invention, les gaz refoulés par le groupe de pompage, sont véhiculés dans une gaine, comprenant une rampe de lavage formant un film d'eau, qui plonge sous le niveau de la nappe d'eau. Les gaz sont donc lavés par précipitation et barbotage.The washing column (10/1) is in the form of a sealed silo stainless steel in which a constant water level is maintained. According to the invention, the gases discharged by the pumping unit are conveyed in a sheath, comprising a washing ramp forming a film of water, which dives below the level of the water table. The gases are therefore washed by precipitation and bubbling.
A la sortie de la colonne de lavage les gaz sont repris et comprimés (11/1) pour leur stockage (12/1) en vue d'une utilisation ultérieure.At the outlet of the washing column the gases are taken up and compressed (11/1) for storage (12/1) for later use.
Les différents éléments décrits ci-dessus sont reliés entre eux par des gaines en acier inoxydable, largement dimensionnées pour éviter d'éventuels colmatage et faciliter la maintenance. Des électrovannes permettent l'automatisation du fonctionnement de l'installation à partir des informations données par les appareils de mesure, de contrôle et d'analyse.The different elements described above are linked together by stainless steel sheaths, large enough to avoid clogging and facilitate maintenance. Solenoid valves allow the automation of the operation of the installation from information given by measuring, control and analysis.
Les besoins en eau de l'installations sont les suivants: l'eau réfrigérante des plaques du condenseur, le maintien du niveau dans la colonne de lavage, l'eau précipitée sur l'enceinte de distillation à refroidir, l'eau de lavage des locaux et des matériels. Par contre on récupère une certaine quantité d'eau après condensation des vapeurs issues de l'enceinte de distillation. Les liquides à traiter proviennent du condenseur, de la colonne de lavage des gaz, du recueil des eaux de propreté des locaux et matériels. L'eau de réfrigération du condenseur est propre et à l'avantage d'être rafraichie. L'eau de refroidissement de l'enceinte est également propre mais peut être chargée de poussières, elle sera filtrée (17/1) avant d'être remise en circuit. Les éléments essentiels constituants le système de traitement des eaux sont: le réservoir destiné à préserver la quantité d'eau adéquate (13/1), l'appareil de réfrigération des plaques du condenseur (14/1), la colonne de lavage (10/1), le bac fitrant de décantation des hydrocarbures (15/1), le tank de stockage des hydrocarbures (16/1), le système piloté par les résultats des analyses d'adjonction de liquide de lavage aux eaux à neutraliser. Ce système est classique à la chimie des eaux et ne fait pas l'objet d'un descriptif particulier. The water requirements of the installations are as follows: cooling water condenser plates, level maintenance in the washing column, the water precipitated on the distillation chamber to be cooled, the water from washing of premises and equipment. By cons we recover some amount of water after condensation of the vapors from the enclosure distillation. The liquids to be treated come from the condenser, the gas washing column, collection of premises clean water and materials. The condenser cooling water is clean and to the advantage to be refreshed. The enclosure cooling water is also clean but can be loaded with dust, it will be filtered (17/1) before being switched back on. The essential components water treatment system are: the tank intended to preserve the correct amount of water (13/1), the appliance for cooling the plates condenser (14/1), the washing column (10/1), the drain pan decanting of hydrocarbons (15/1), the oil storage tank (16/1), the system driven by the results of the addition analyzes of washing liquid to the waters to be neutralized. This system is classic to water chemistry and is not the subject of a particular description.
Les éléments solides résiduels sont d'une part, déversés sur un convoyeur (23/1), d'autre part, pour les charbons, aspirés (24/1) et mis en silo (25/1). Les matériaux lourds rendus propres sont acheminés vers un tri (26-27-28-29/1) classique aux industries de la récupération.On the one hand, the residual solid elements are discharged onto a conveyor (23/1), on the other hand, for coals, sucked up (24/1) and put in silo (25/1). Heavy materials returned clean are sent to sorting (26-27-28-29 / 1) classic for the recovery industries.
Le suivi et la gestion de l'exploitation sont assurés, d'une façon continue, par un ensemble d'appareils dont le choix et la redondance garantissent la fiabilité du fonctionnement de l'installation.The follow-up and the management of the exploitation are ensured, in a way continuous, by a set of devices whose choice and redundancy guarantee the reliability of the operation of the installation.
Selon l'invention, on distingue quatre types de mesures à effectuer: les mesures de fonctionnement qui déclenche les différentes phases du procédé, les mesures de sécurité devant assurer la protection du matériel et par conséquent du personnel, les mesures de qualité devant garantir et prouver le respect de l'environnement, les mesures de rentabilité de l'installation.According to the invention, there are four types of measurements to be made: the operating measures which trigger the different phases of the security measures to protect the equipment and therefore personnel, the quality measures to guarantee and demonstrate respect for the environment, profitability measures installation.
Les mesures sont effectuées par des sondes ou capteurs qui sont associés à des appareils de contrôle ou de commande. En outre, certaines mesures jugées primordiales, sont archivées sous une forme graphique ou sous forme de messages alphanumériques. Cet archivage assure une aide à la maintenance des matériels et la conservation de l'historique des traitements. La gestion de l'ensemble de l'installation est confiée à un automate programmable, le suivi des mesures en temps réel ou différé est assuré par un système de visualisation informatisé.The measurements are carried out by probes or sensors which are associated to monitoring or control apparatus. In addition, certain measures deemed essential, are archived in graphic form or in alphanumeric messages. This archiving ensures maintenance assistance of materials and the conservation of the treatment history. Management of the entire installation is entrusted to a programmable controller, real-time or delayed measurement monitoring is ensured by a system computerized visualization.
Les mesures de fonctionnement concernent: la température interne de l'enceinte de distillation qui est prise en compte par un régulateur/programmateur qui lui-même pilote l'unité de puissance à thyristors, la valeur de la dépression dans l'enceinte qui déclenche la mise en service du chauffage, le débit des gaz aspirés, la température en amont du groupe de pompage, le niveau des liquides recueillis à la base du condenseur, le niveau dans la colonne de lavage, le taux de remplissage des réservoirs.The operating measurements relate to: the internal temperature of the distillation chamber which is taken into account by a regulator / programmer which itself controls the power unit to thyristors, the value of the depression in the enclosure that triggers the start-up of the heating system, the flow of aspirated gases, the temperature upstream of the pumping unit, the level of liquids collected at the base of the condenser, the level in the washing column, the rate of filling tanks.
Les mesures de sécurité concernent: la température des éléments chauffants du four pour éviter des surchauffes préjudiciables à la tenue du matériel dans le temps, les pressions internes du condenseur et de la colonne de lavage, les débits des gaz en entrée et en sortie du condenseur, la température de réfrigération des plaques du condenseur.The safety measures concern: the temperature of the heating elements of the oven to avoid overheating detrimental to the performance of the equipment over time, the internal pressures of the condenser and the washing, the gas flow rates at the inlet and outlet of the condenser, the refrigeration temperature of the condenser plates.
Les mesures de qualité concernent: l'analyse des gaz incondensables, l'analyse des eaux recyclées, l'analyse de l'atmosphère du local, la température et le débit de l'eau devant être rejetée à l'égout.Quality measures concern: analysis of noncondensable gases, analysis of recycled water, analysis of the local atmosphere, temperature and flow of water to be discharged to the sewer.
Les mesures de rentabilité concernent: le poids des produits à traiter, la consommation en énergie électrique et la consommation en eau de ville. Ces mesures permettrons d'établir un bilan d'exploitation.The profitability measures concern: the weight of the products to be treated, consumption of electrical energy and consumption of city water. These measures will make it possible to establish an operating balance sheet.
Claims (3)
- Facility featuring a heat low temperature and partial vacuum treatment for industrial, hospital, household and similar waste, whether they be solid, liquid or gas, achieving higher environment protection than standard provisions.
The facility includes the following distinctive featuresa mobile heat processing furnace moving from one sealed cell to the other (3/1)two sealed distillation cells (2/1)a distillation gas condenser (7/1)a vacuum unit for both sealed cells (9/1)a non condensable gas (10/1) cleaning column for gas from the condenser (7/1)a gas cleaning water processing system (15/1)a sorting system for solid effluent items from the heat process (24-26/1)automatic heat treatment cycle programming - Facility in accordance with the designation of claim 1, characterised in that the heat treatment furnace is mobile, made up of a rolling motorised vault moving on rails. The vault is closed at both ends by lifting doors referred to as "guillotines". The high position of the doors allows the furnace to move from one distillation cell to the other. In order to achieve convection heat, the most efficient in those temperature ranges (500 °C), the furnace has a turbine forcing room air onto the electric heaters.
- Facility, in accordance with the designation of claims 1 and 2, characterised in that both sealed distillation cells (2/1) rest on refractory concrete bases. The stainless steel cells receive the treatment produces and depending on the position of the furnace, are subjected to the heating phase by the electric heaters located in the furnace, or to the cooling phase, by exposing the cell to open air as the furnace moves to the second cell, and to sprayed water. The cell door turns on an axis and comes to be parallel with the front side, equipped with a joint, which it is pushed up against by a system of slanting blocks and catches.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9603043 | 1996-03-11 | ||
| FR9603043A FR2745819B1 (en) | 1996-03-11 | 1996-03-11 | INSTALLATION FOR HEAT TREATMENT OF INDUSTRIAL, HOSPITAL, HOUSEHOLD AND SIMILAR WASTE WITH ENVIRONMENTAL PROTECTION BEYOND FIXED STANDARDS |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0795594A1 EP0795594A1 (en) | 1997-09-17 |
| EP0795594B1 true EP0795594B1 (en) | 2003-02-19 |
Family
ID=9490064
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP19970400483 Expired - Lifetime EP0795594B1 (en) | 1996-03-11 | 1997-03-03 | Plant for the environmentally friendly thermal treatment of industrial, hospital, domestic and the like waste |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0795594B1 (en) |
| DE (1) | DE69719102D1 (en) |
| ES (1) | ES2205142T3 (en) |
| FR (1) | FR2745819B1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008075931A1 (en) * | 2006-12-20 | 2008-06-26 | Rodriguez Hernandez Jesus Edua | System and method for obtaining hydrocarbons, from organic and inorganic solid waste |
| DE102014007595A1 (en) * | 2014-05-26 | 2015-11-26 | Hilmar Hubbes | Process for the treatment of polymeric waste |
| CN110594747B (en) * | 2019-10-16 | 2024-07-12 | 中国海关科学技术研究中心 | Cross-border biological product comprehensive quarantine treatment equipment and application method thereof |
| CN117128714B (en) * | 2023-10-26 | 2024-01-12 | 杭州特盈低温液化装备有限公司 | Low-power consumption air separation device |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2132220A (en) * | 1982-12-10 | 1984-07-04 | Kameda Works Limited Company | Treating method for the industrial waste products under the dry distillation |
| FR2674149B1 (en) * | 1991-03-20 | 1994-04-15 | Pierre Chaussonnet | SYSTEM FOR THE TREATMENT BY THERMOLYSIS, IN TOTAL OXYGEN ABSENCE OF SOLID PRODUCTS WHOSE REJECTION IS HARMFUL FOR THE ENVIRONMENT. |
| DE4202321A1 (en) * | 1992-01-29 | 1993-08-05 | Adolf Gorski | Low temp. carbonisation of waste materials - in series of 3 chambers for filling, carbonisation and cooling, with afterburner, has low energy requirement and high throughput |
| US5366595A (en) * | 1993-05-11 | 1994-11-22 | Padgett Michael A | Mobile apparatus for pyrolyzing carbonaceous material and related method |
| EP0630957B1 (en) * | 1993-06-23 | 1998-09-09 | Rémy Gourhan | Low-pressure pyrolysis furnace for the destructions of organic industrial waste |
-
1996
- 1996-03-11 FR FR9603043A patent/FR2745819B1/en not_active Expired - Fee Related
-
1997
- 1997-03-03 DE DE69719102T patent/DE69719102D1/en not_active Expired - Lifetime
- 1997-03-03 EP EP19970400483 patent/EP0795594B1/en not_active Expired - Lifetime
- 1997-03-03 ES ES97400483T patent/ES2205142T3/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| FR2745819B1 (en) | 1999-04-09 |
| FR2745819A1 (en) | 1997-09-12 |
| DE69719102D1 (en) | 2003-03-27 |
| ES2205142T3 (en) | 2004-05-01 |
| EP0795594A1 (en) | 1997-09-17 |
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