EP0413813A1 - Devices for treating human or animal dejections by means of micro-waves. - Google Patents

Devices for treating human or animal dejections by means of micro-waves.

Info

Publication number
EP0413813A1
EP0413813A1 EP90905203A EP90905203A EP0413813A1 EP 0413813 A1 EP0413813 A1 EP 0413813A1 EP 90905203 A EP90905203 A EP 90905203A EP 90905203 A EP90905203 A EP 90905203A EP 0413813 A1 EP0413813 A1 EP 0413813A1
Authority
EP
European Patent Office
Prior art keywords
materials
microwave
treated
tank
solid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP90905203A
Other languages
German (de)
French (fr)
Other versions
EP0413813B1 (en
Inventor
Maurice Lataillade
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to AT90905203T priority Critical patent/ATE96486T1/en
Publication of EP0413813A1 publication Critical patent/EP0413813A1/en
Application granted granted Critical
Publication of EP0413813B1 publication Critical patent/EP0413813B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/32Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
    • F26B3/34Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
    • F26B3/347Electromagnetic heating, e.g. induction heating or heating using microwave energy
    • EFIXED CONSTRUCTIONS
    • E03WATER SUPPLY; SEWERAGE
    • E03DWATER-CLOSETS OR URINALS WITH FLUSHING DEVICES; FLUSHING VALVES THEREFOR
    • E03D11/00Other component parts of water-closets, e.g. noise-reducing means in the flushing system, flushing pipes mounted in the bowl, seals for the bowl outlet, devices preventing overflow of the bowl contents; devices forming a water seal in the bowl after flushing, devices eliminating obstructions in the bowl outlet or preventing backflow of water and excrements from the waterpipe
    • E03D11/02Water-closet bowls ; Bowls with a double odour seal optionally with provisions for a good siphonic action; siphons as part of the bowl
    • E03D11/11Bowls combined with a reservoir, e.g. containing apparatus for disinfecting or for disintegrating

Definitions

  • the present invention relates to the treatment of human or animal droppings and aims to propose a new microwave treatment technique capable of solving the sanitation problems posed by the elimination of said droppings and, more particularly, of reducing very substantially the risks of pollution and other nuisances specific to this type of discharge, independently and economically.
  • the subject of the invention is a method for treating human or animal excrement by microwaves, characterized in that it consists in subjecting at least the solid parts of the excreta to be treated to irradiation by microwaves in conditions controlled so that at the end of processing of said parts they have reached a predetermined degree of desiccation.
  • the excreta to be treated namely the solid parts alone or in mixture with the liquid parts, are forced to pass through a determined space subjected to microwave irradiation, under determined flow conditions so as to obtain the desired degree of desiccation of the materials treated on leaving the irradiation zone.
  • the water vapor released during the microwave treatment is collected with a view to possible recycling or recovery of the condensation water.
  • the said desiccated materials are collected and conditioned for their elimination or for further treatment.
  • the liquid parts are separated before the treatment and subjected to evaporation to collect the water with a view to its possible recycling or recovery.
  • the invention also relates to devices for implementing the above method.
  • Such a process is remarkably effective and makes it possible to transform, according to a closed circuit and therefore autonomous process, polluting products and generators of various nuisances into dry, sterile residues, of reduced volume and easily handled for their evacuation.
  • the method allows the recovery of the water contained in the manure and in particular its recycling in the system for collecting manure, thus contributing to ensuring autonomy which can be total at the installation for treating manure, this substantial advantage of the method of the invention being particularly advantageous in its application to the treatment of droppings in sites with high temporary traffic which are not generally equipped in particular with the required water facilities, or in sites comprising large volumes to be treated and sterilized, such as animal husbandry, or on board air, land or sea vehicles.
  • Figure 1 is a schematic perspective view of an installation for processing human excrement implementing the method of the invention
  • Figure 2 is a partial vertical sectional view of another embodiment of the method of
  • Figure 3 is a schematic axial vertical sectional view of the module of the installation of Figure 1 where the solid / liquid separation takes place for microwave treatment of solids, and
  • FIG 4 illustrates diagrammatically an installation according to the invention intended for the treatment of large quantities of excrement.
  • Figure 1 there is shown schematically an embodiment of the method of the invention applied to the treatment of human excrement collected from a bowl of
  • the bowl 1 is connected by a pipe 2 in a slight downward slope to a tank 3 for solid / liquid separation.
  • the tank 3 is connected by a pipe 4 to the lower part of a module 5 for conveying solid materials coming from the tank 3 upwards in the direction of a microwave irradiation unit 6.
  • a microwave irradiation unit 6 Above the irradiation unit 6 is arranged an extractor 7 of the gases generated during the microwave treatment.
  • the solid materials coming from the treatment unit 6 are conveyed through the extractor 7 by a conduit 8 which leads to a tank 9 for recovering the desiccated treated materials.
  • the extractor 7 consists of an enclosure surrounding the duct 8 and intended to recover the vapors conveyed in the duct 8 and which escape therefrom at the level of the extractor 7 by passages provided for this purpose in the wall of the said duct 8.
  • the vapors collected are conveyed by an insulated pipe 10 in a tank 11 for condensing the vapors into water. Condensation takes place at atmospheric pressure, the tank 11 being vented through a chimney 12 comprising a filter (not shown), an extractor fan 13 and a ventilation cap 14.
  • the tank 9 is an enclosure into which the duct 8 opens after passing through the extractor 7.
  • the tank 9 is provided with an access hatch 15 allowing the insertion into the tank of a bag for collecting the desiccated materials conveyed through said conduit 8.
  • the enclosure of the tank 9 is connected by an insulated pipe 16 to the chimney 12.
  • the pipeline collects residual vapors at
  • the tank 11 is also connected by a pipe 17, optionally provided with a filter 18 and a booster 19, to the bowl 1 in order to reuse the condensed water for emptying and cleaning the bowl.
  • the tank 3 is also provided with vents 20, a conduit
  • the tank 25 is provided with vents 26, a gas evacuation duct 27 and a pipe 28 for supplying the vapors to the condensation tank 11.
  • a bypass 29 provided with a valve 30 for regulating steam connects the pipe 28 to the chimney 12, upstream of the filter.
  • the assembly 5-6 of FIG. 1 is, for example, in accordance with the device represented diagrammatically in FIG. 2.
  • FIG. 2 a vertical cylindrical duct has been shown at 31 in which an Archimedes screw 32 is disposed, moved by a geared motor assembly symbolized by
  • the conduit 31 passes through an annular enclosure 34 forming a waveguide or applicator and concentrating the microwaves emitted by a generator 35 on the material passing through the interior of the said conduit 31, the wall of which is made of a suitable material, for example " Teflon ", transparent to microwaves.
  • FIG. 1 may include a processing unit 6 consisting of an applicator 34 and a generator
  • a module 5 for conveying the materials to be treated in a conduit 31 comprising a vertical Archimedes screw 32 actuated by example by an electric motor 36 via an appropriate transmission 37.
  • the screw 32 continuously pushes the solid materials in the conduit 31 in the direction of the microwave applicator 34.
  • the materials undergo irradiation with microwaves such that at the exit from the irradiated area the materials are in the desired dissection state.
  • the microwave generator 35 and its applicator 34 are known devices. One can use for example as an applicator those described in EP-0.252.542 or any other system with rectangular or square section forming a treatment cavity, in accordance with the standards in force, in particular concerning microwave leaks.
  • microwave leak sensors are provided, on the one hand, near the generator 35 and, on the other hand, in the passenger compartment where the bowl 1 is installed.
  • the frequency of the microwave generator is for example of
  • the power of the microwave generation unit is calculated so that it allows the desired degree of drying of the treated materials, the flow rate of the latter in the zone of the conduit 31 passing through the applicator (s) 34, determined and regulated by the speed of rotation of the screw 32, also being an essential parameter of the microwave treatment.
  • the desiccated materials are conveyed through the conduit 8 by the thrust exerted by the underlying materials themselves pushed by the screw 32, in the direction of the extractor 7 responsible for collecting the vapor d water generated during material processing.
  • the desiccated materials are pushed into the tank 9 where they are bagged like dust in a vacuum cleaner bag.
  • the desiccated materials are enclosed in a waterproof bag which is easy to handle with a view to its evacuation or a possible subsequent recovery treatment.
  • the desiccated materials are stored in the reservoir 38 and recovered by means of an inspection hatch 45.
  • the unit 5 receives only the solids from tank 3.
  • FIG. 3 schematically shows an embodiment of such a tank.
  • This consists of a cylindrical enclosure 46 of vertical axis, provided in its center with an access hatch 47 allowing in particular the installation of a central cylindrical filter 48.
  • the internal annular space of the enclosure 46 is divided into two parts by a grid 49 of tron ⁇ onic shape delimiting a lower space 50 for collecting the liquid part 51 (urine and water) droppings and a higher space
  • the droppings (solid / liquid mixture) are introduced into the enclosure 46 by a conduit (2 in the embodiment of FIG. 1) or by several if the same installation treats the droppings from several bowls 1 connected to the same tank 3 .
  • the liquid part 51 is evacuated through the conduit 23 connected to said evaporation tank 25.
  • the solid part 53 is directed through the conduit 4 to the processing unit (5,6). It should be noted that the inclination of the grid 49 tends to push the solid materials 53 outwards towards the orifice of the duct 4 by a wedge effect.
  • the evaporation tank 25 the structure and operation of which are well known, makes it possible to recover the water by condensation of the steam supplied by the pipe 28 into the condensation tank 11.
  • the water thus recovered is advantageously recycled to the bowl 1 for example, which makes it possible to operate the installation independently without the need to connect it to an external water supply network.
  • a simple make-up water tank (not shown) can be provided in the installation.
  • the liquid part is evacuated by gravity at the lower end of the duct 31, via the pipe 41.
  • the screw 32 is automatically put into service thanks to a material presence sensor disposed near the outlet of the conduit (4, Figure 1; 2, Figure 2) for introducing the materials to be treated into the housing. of screw 32, such a sensor being symbolized at 54 on Figure 2 and connected (55) to the gear motor assembly 33
  • Such a sensor 54 can be placed in the tank 3 (FIG. 3) at a suitable location.
  • the liquid materials can be separated before introduction into the module 5 by any appropriate means, with recovery and recycling of the water or simple elimination.
  • the solid / liquid mixture can be treated without separation in unit 6, the microwave generator (s) being adjusted accordingly, the water vapors collected by the extractor 7 and additionally by the enclosure 9 being simply greater in quantity.
  • the condensed water is either recovered and recycled, or eliminated by any appropriate means.
  • FIG. 4 illustrates a variant application of the method of the invention to the treatment of large quantities of excrement and very particularly of animal excrement.
  • FIG. 4 schematically represents a cascade treatment installation comprising a hopper 56 for receiving the materials (solids and mixed liquids) to be treated, a hopper 57 for receiving the desiccated materials after microwave treatments operated in a plurality of units in series 58a, 58b, etc. in variable number.
  • Each unit 58a, 58b, etc. comprises at least one horizontal conveying conduit 59 provided for example with an Archimedes screw similar to that of the device in FIG. 2, driven by a geared motor 60.
  • Each conduit 59 connects an upstream hopper to a downstream hopper.
  • Figure 4 are shown, in addition to the two end hoppers 56, 57, two intermediate hoppers 61 and 62 respectively.
  • Each duct 59 is equipped with at least one generator-microwave appli ⁇ ator 63 and at least one vapor extractor 64 surrounding the duct 59 which is, at this level, provided with perforations or the like in its wall for the extraction of vapors.
  • the extractors 64 are connected by conduits 65 to a condensing unit (not shown) for the recovery and possible recycling of the water extracted from the treated materials.
  • each unit 58a, 58b, etc ... comprises a single conduit 59, a single generator-applicator assembly 63 and a single extractor 64, but one can provide a single conduit 59 and several devices 63 and 64 side by side, or else several conduits 59 in parallel with each one or more devices 63 and one or more devices 64.
  • the extractor device 64 can be constituted for example by a microwave application chamber of the type equipping the device 63 and whose inlet, instead of being connected to a microwave generator, would be connected to the extraction duct 65, the duct 59 being of course provided with perforations or passages in its wall at the level of this application chamber .
  • Each intermediate hopper 61, 62 has, in the upper part, a discharge orifice for the conduit 59 of the upstream processing unit and, in the lower part, the conveying screw of the downstream processing unit.
  • each intermediate hopper 61, 62 is capped with a vapor extraction manifold 66 also connected to said condensing unit.
  • the parameters of the processing units 58a, 58b, et ⁇ ..., namely frequency of the microwaves, flow of materials in the conduit (s) 59, are adjusted so that the material discharged into the final hopper 57 has the degree of desired desiccation, the degrees of desiccation of the materials in the intermediate hoppers 61, 62 being intermediate between those of the respectively initial and final states of the materials treated.
  • the desiccated materials are in bulk in the hopper (s) 57 and are evacuated by any appropriate means for the purpose of elimination, reprocessing or recycling.
  • any other means than an Archimedes' screw for conveying, under the conditions of controlled flow, the materials to be treated into the microwave application space which space can have a different geometric configuration according to the nature of the conveying means and the morphology of the material conveying conduit.
  • the solid / gas separation downstream of the microwave treatment can be carried out in another way than by steam extraction and condensation of water at atmospheric pressure, in the known manner, as is the case. case in the installation of figure 1.

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Health & Medical Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Biotechnology (AREA)
  • Electromagnetism (AREA)
  • Molecular Biology (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Hydrology & Water Resources (AREA)
  • Public Health (AREA)
  • Biomedical Technology (AREA)
  • Treatment Of Sludge (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Drying Of Solid Materials (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fats And Perfumes (AREA)
  • Non-Flushing Toilets (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

Pour transformer les déjections en résidus secs et stériles, ces matières sont soumises aux radiations micro-ondes dans une unité de traitement (6). Un séparateur solides/liquides (3) peut être incorporé en amont de l'unité de traitement. Le circuit d'évacuation des liquides comporte une cuve d'évaporation (25), un circuit de récupération de vapeur d'eau (28), une cuve de condensation (11) et un circuit de recyclage (17, 18, 19) de l'eau de condensation.To transform the droppings into dry and sterile residues, these materials are subjected to microwave radiation in a treatment unit (6). A solid / liquid separator (3) can be incorporated upstream of the treatment unit. The liquid evacuation circuit includes an evaporation tank (25), a water vapor recovery circuit (28), a condensation tank (11) and a recycling circuit (17, 18, 19) of condensation water.

Description

PROCEDE DE TRAITEMENT DES DEJECTIONS HUMAINES OU ANIMALES PAR MICRO-ONDES ET DISPOSITIFS POUR SA MISE EN OEUVRE PROCESS FOR TREATING HUMAN OR ANIMAL DEJECTION BY MICROWAVE AND DEVICES FOR CARRYING OUT IT
La présente invention se rapporte au traitement des déjections humaines ou animales et vise à proposer une nouvelle technique de traitement par micro-ondes propre à résoudre les problèmes d'assainissement posés par l'élimination desdites déjections et, plus particulièrement, à réduire très substantiellement les risques de pollution et autres nuisances spécifiques à ce type de rejets et, ce, de manière autonome et économique.The present invention relates to the treatment of human or animal droppings and aims to propose a new microwave treatment technique capable of solving the sanitation problems posed by the elimination of said droppings and, more particularly, of reducing very substantially the risks of pollution and other nuisances specific to this type of discharge, independently and economically.
A cet effet, l'invention a pour objet un procédé de traitement des déjections humaines ou animales par micro-ondes, caractérisé en ce qu'il consiste à soumettre au moins les parties solides des déjections à traiter à une irradiation par micro-ondes dans des conditions contrôlées en sorte qu'en fin de traitement desdites parties celles-ci aient atteint un degré de dessication prédéterminé.To this end, the subject of the invention is a method for treating human or animal excrement by microwaves, characterized in that it consists in subjecting at least the solid parts of the excreta to be treated to irradiation by microwaves in conditions controlled so that at the end of processing of said parts they have reached a predetermined degree of desiccation.
Suivant un mode de mise en oeuvre du procédé, les déjections à traiter, à savoir les parties solides seules ou en mélange avec les parties liquides, sont contraintes de défiler dans un espace déterminé soumis aux irradiations micro-ondes, dans des conditions de débit déterminées de façon à obtenir le degré désiré de dessication des matières traitées à la sortie de la zone d'irradiation.According to an embodiment of the method, the excreta to be treated, namely the solid parts alone or in mixture with the liquid parts, are forced to pass through a determined space subjected to microwave irradiation, under determined flow conditions so as to obtain the desired degree of desiccation of the materials treated on leaving the irradiation zone.
Par ailleurs, avantageusement on recueille la vapeur d'eau dégagée au cours du traitement aux micro-ondes en vue d'un éventuel recyclage ou récupération de l'eau de condensation. Egalement, avantageusement on recueille lesdites matières dessiquées et on les conditionne en vue de leur élimination ou d'un traitement ultérieur.Furthermore, advantageously, the water vapor released during the microwave treatment is collected with a view to possible recycling or recovery of the condensation water. Also, advantageously, the said desiccated materials are collected and conditioned for their elimination or for further treatment.
Dans le cas où seules les parties solides sont traitées aux micro-ondes, les parties liquides sont séparées avant le traitement et soumise à évaporation pour recueillir l'eau en vue de son éventuel recyclage ou récupération.In the case where only the solid parts are treated in the microwave, the liquid parts are separated before the treatment and subjected to evaporation to collect the water with a view to its possible recycling or recovery.
L'invention a également pour objet des dispositifs pour la mise en oeuvre du procédé ci-dessus. Un tel procédé est remarquablement efficace et permet de transformer, selon un processus en circuit fermé et donc autonome, des produits polluants et générateurs de nuisances diverses en résidus secs, stériles, de volume réduit et facilement manipulables pour leur évacuation. En outre, le procédé permet la récupération des eaux contenues dans les déjections et en particulier leur recyclage dans le système de collecte des déjections, contribuant ainsi à assurer une autonomie pouvant être totale à l'installation de traitement des déjections, cet avantage substantiel du procédé de l'invention étant particulièrement intéressant dans son application au traitement des déjections dans des sites à forte fréquentation temporaire qui ne sont pas généralement équipés notamment des facilités en eau requises, ou dans des sites comportant d'importants volumes à traiter et stériliser, tels que des élevages d'animaux, ou encore à bord de véhicules aériens, terrestres ou maritimes.The invention also relates to devices for implementing the above method. Such a process is remarkably effective and makes it possible to transform, according to a closed circuit and therefore autonomous process, polluting products and generators of various nuisances into dry, sterile residues, of reduced volume and easily handled for their evacuation. In addition, the method allows the recovery of the water contained in the manure and in particular its recycling in the system for collecting manure, thus contributing to ensuring autonomy which can be total at the installation for treating manure, this substantial advantage of the method of the invention being particularly advantageous in its application to the treatment of droppings in sites with high temporary traffic which are not generally equipped in particular with the required water facilities, or in sites comprising large volumes to be treated and sterilized, such as animal husbandry, or on board air, land or sea vehicles.
D'autres caractéristiques et avantages ressortiront de la description qui va suivre de modes de mise en oeuvre du procédé de l'invention, description donnée à titre d'exemple uniquement et en regard des dessins annexés sur lesquels :Other characteristics and advantages will emerge from the following description of modes of implementing the method of the invention, description given by way of example only and with reference to the appended drawings in which:
Figure 1 est une vue en perspective schématique d'une installation de traitement de déjections humaines mettant en oeuvre le procédé de l'invention ; Figure 2 est une vue en coupe verticale partielle d'un autre mode de mise en oeuvre du procédé deFigure 1 is a schematic perspective view of an installation for processing human excrement implementing the method of the invention; Figure 2 is a partial vertical sectional view of another embodiment of the method of
1'invention ;The invention;
Figure 3 est une vue en coupe verticale axiale schématique du module de l'installation de la figure 1 où s'opère la séparation solides/liquides préala- blement au traitement aux micro-ondes des matières solides, etFigure 3 is a schematic axial vertical sectional view of the module of the installation of Figure 1 where the solid / liquid separation takes place for microwave treatment of solids, and
Figure 4 illustre sσhématiquement une installation conforme à l'invention destinée au traitement de quantités importantes de déjections.Figure 4 illustrates diagrammatically an installation according to the invention intended for the treatment of large quantities of excrement.
Sur la figure 1 on a représenté schématiquement un mode de mise en oeuvre du procédé de l'invention appliqué au traitement de déjections humaines collectées à partir d'un cuvette deIn Figure 1 there is shown schematically an embodiment of the method of the invention applied to the treatment of human excrement collected from a bowl of
WC 1. La cuvette 1 est reliée par une canalisation 2 en légère pente descendante à une cuve 3 de séparation solides/liquides.WC 1. The bowl 1 is connected by a pipe 2 in a slight downward slope to a tank 3 for solid / liquid separation.
La cuve 3 est reliée par une canalisation 4 à la partie inférieure d'un module 5 d'acheminement des matières solides provenant de la cuve 3 vers le haut en direction d'une unité 6 d'irradiation par micro-ondes. Au-dessus de l'unité 6 d'irradiation est disposé un extracteur 7 des gaz générés lors du traitement aux micro-ondes.The tank 3 is connected by a pipe 4 to the lower part of a module 5 for conveying solid materials coming from the tank 3 upwards in the direction of a microwave irradiation unit 6. Above the irradiation unit 6 is arranged an extractor 7 of the gases generated during the microwave treatment.
Plus précisément, les matières solides en provenance de l'unité de traitement 6 sont acheminées au travers de l'extracteur 7 par un conduit 8 qui aboutit à une cuve 9 de récupération des matières traitées dessiquees.More specifically, the solid materials coming from the treatment unit 6 are conveyed through the extractor 7 by a conduit 8 which leads to a tank 9 for recovering the desiccated treated materials.
L'extracteur 7 est constitué d'une enceinte entourant le conduit 8 et destinée à récupérer les vapeurs véhiculées dans le conduit 8 et qui s'en échappent à hauteur de l'extracteur 7 par des passages ménagés à cet effet dans la paroi dudit conduit 8. Les vapeurs recueillies sont acheminées par une canalisation calorifugée 10 dans une cuve 11 de condensation des vapeurs en eau. La condensation s'effectue à la pression atmosphérique, la cuve 11 étant mise à l'atmosphère par une cheminée 12 comportant un filtre (non représenté), un extrateur-ventilateur 13 et un chapeau de ventilation 14.The extractor 7 consists of an enclosure surrounding the duct 8 and intended to recover the vapors conveyed in the duct 8 and which escape therefrom at the level of the extractor 7 by passages provided for this purpose in the wall of the said duct 8. The vapors collected are conveyed by an insulated pipe 10 in a tank 11 for condensing the vapors into water. Condensation takes place at atmospheric pressure, the tank 11 being vented through a chimney 12 comprising a filter (not shown), an extractor fan 13 and a ventilation cap 14.
La cuve 9 est une enceinte dans laquelle débouche le conduit 8 après traversée de l'extracteur 7. La cuve 9 est munie d'une trappe d'accès 15 permettant l'insertion dans la cuve d'un sac de recueil des matières dessiquees acheminées par ledit conduit 8.The tank 9 is an enclosure into which the duct 8 opens after passing through the extractor 7. The tank 9 is provided with an access hatch 15 allowing the insertion into the tank of a bag for collecting the desiccated materials conveyed through said conduit 8.
L'enceinte de la cuve 9 est reliée par une canalisation calorifugée 16 à la cheminée 12. La canalisation recueille les vapeurs résiduelles àThe enclosure of the tank 9 is connected by an insulated pipe 16 to the chimney 12. The pipeline collects residual vapors at
1'intérieur de la cuve 9 et les évacue avec retour de l'eau de condensation vers la cuve 11.Inside the tank 9 and evacuates them with return of the condensation water to the tank 11.
La cuve 11 est par ailleurs reliée par une canalisation 17, munie éventuellement d'un filtre 18 et d'un surpresseur 19, à la cuvette 1 afin de réutiliser l'eau condensée pour le vidage et le nettoyage de la cuvette.The tank 11 is also connected by a pipe 17, optionally provided with a filter 18 and a booster 19, to the bowl 1 in order to reuse the condensed water for emptying and cleaning the bowl.
La cuve 3 est par ailleurs munie d'évents 20, d'un conduitThe tank 3 is also provided with vents 20, a conduit
21 d'évacuation de gaz, d'une trappe d'accès 22 et d'un conduit 23 équipé d'un manchon de filtrage 24 chargé d'acheminer les parties liquides en provenance de la cuve 3 vers une cuve d'évaporation 25. Cette cuve, de conception classique, est équipée de résistances chauffantes électriques plongeantes chargées d'évaporer l'eau contenue dans le mélange eaux-urines provenant de la cuve de séparation 3.21 for discharging gas, an access hatch 22 and a conduit 23 equipped with a filtering sleeve 24 responsible for conveying the liquid parts coming from the tank 3 towards an evaporation tank 25. This tank, of conventional design, is fitted with plunging electric heating resistors responsible for evaporating the water contained in the water-urine mixture coming from the separation tank 3.
La cuve 25 est munie d'évents 26, d'un conduit d'évacuation des gaz 27 et d'une canalisation 28 d'amenée des vapeurs dans la cuve de condensation 11. Une dérivation 29 munie d'une vanne 30 de régulation de vapeur relie la canalisation 28 à la cheminée 12, en amont du filtre.The tank 25 is provided with vents 26, a gas evacuation duct 27 and a pipe 28 for supplying the vapors to the condensation tank 11. A bypass 29 provided with a valve 30 for regulating steam connects the pipe 28 to the chimney 12, upstream of the filter.
L'ensemble 5-6 de la figure 1 est par exemple conforme au dispositif représenté sσhématiquement sur la figure 2.The assembly 5-6 of FIG. 1 is, for example, in accordance with the device represented diagrammatically in FIG. 2.
Sur cette figure 2 on a représenté en 31 un conduit vertical cylindrique dans lequel est disposée une vis d'Archimède 32 mue par un ensemble moto-réducteur symbolisé enIn this FIG. 2, a vertical cylindrical duct has been shown at 31 in which an Archimedes screw 32 is disposed, moved by a geared motor assembly symbolized by
33.33.
Le conduit 31 traverse une enceinte annulaire 34 formant guide ou applicateur d'ondes et concentrant les micro-ondes émises par un générateur 35 sur la matière transitant à l'intérieur dudit conduit 31 dont la paroi est en un matériau approprié, par exemple du "Téflon", transparent vis à vis des micro-ondes.The conduit 31 passes through an annular enclosure 34 forming a waveguide or applicator and concentrating the microwaves emitted by a generator 35 on the material passing through the interior of the said conduit 31, the wall of which is made of a suitable material, for example " Teflon ", transparent to microwaves.
La vis d'Archimède 32 ne s'étend pas jusqu'à l'applicateur de micro-ondes 34. L'installation de la figure 1 peut comporter une unité de traitement 6 constituée d'un applicateur 34 et d'un générateurArchimedes' screw 32 does not extend to the microwave applicator 34. The installation of FIG. 1 may include a processing unit 6 consisting of an applicator 34 and a generator
35 tels que représentés sur la figure 2 et un module 5 d'acheminement dans un conduit 31 des matières à traiter comprenant une vis d'Archimède 32 verticale actionnée par exemple par un moteur électrique 36 par l'intermédiaire d'une transmission appropriée 37.35 as shown in FIG. 2 and a module 5 for conveying the materials to be treated in a conduit 31 comprising a vertical Archimedes screw 32 actuated by example by an electric motor 36 via an appropriate transmission 37.
Dans le mode de réalisation de la figure 2, le conduit 31, après traversée de l'applicateur 34, débouche dans un réservoir étanσhe 38 mis à l'atmosphère par un conduit 39 muni d'un filtre 40.In the embodiment of FIG. 2, the duct 31, after crossing the applicator 34, opens into a etanσhe reservoir 38 vented by a duct 39 provided with a filter 40.
Toujours dans le mode de réalisation de la figure 2 et contrairement au mode de réalisation de la figure 1, la totalité des parties solides et liquides des déjections amenées par gravité par la canalisation 2 en provenance de la cuvette 1, est admise dans le module 31-32 d'acheminement des matières vers la zone de traitement aux micro-ondes. Toutefois, seules les matières solides sont prises en charge par la vis 32, la partie liquide étant évacuée à la partie inférieure du conduit 31 par une canalisation 41 en direction d'une cuve d'évaporation 42 analogue à la cuve 25 de la figure 1 et munie d'un conduit 43 d'évacuation des vapeurs avec filtre 44.Still in the embodiment of FIG. 2 and contrary to the embodiment of FIG. 1, all of the solid and liquid parts of the excrement brought by gravity by the pipe 2 coming from the bowl 1, is admitted into the module 31 -32 routing of materials to the microwave treatment area. However, only the solid materials are taken up by the screw 32, the liquid part being evacuated to the lower part of the conduit 31 by a pipe 41 in the direction of an evaporation tank 42 similar to the tank 25 of FIG. 1 and provided with a pipe 43 for discharging the vapors with filter 44.
Le fonctionnement des moyens d'acheminement (5,31,32) des figures 1 et 2 des matières solides en direction de l'espace, délimité à l'intérieur du conduit 31, à hauteur de l'applicateur micro-ondes 34, d'irradiation desdites matières par des micro-ondes appropriées est le suivant.The operation of the conveying means (5,31,32) of FIGS. 1 and 2 of the solid materials in the direction of the space, delimited inside the conduit 31, up to the microwave applicator 34, d irradiation of said materials with suitable microwaves is as follows.
La vis 32 pousse de manière continue les matières solides dans le conduit 31 en direction de l'applicateur à micro-ondes 34. Au cours de la traversée de la zone du conduit 31 entourée par l'applicateur 34, les matières subissent une irradiation aux micro-ondes telles qu'à la sortie de la zone irradiée les matières soient dans l'état de dissécation désiré. Dans la présente application, il est souhaitable d'avoir des matières aussi sèches que possible afin de réduire le volume des déchets solides, et de faciliter leur manipulation ou conditionnement ultérieur.The screw 32 continuously pushes the solid materials in the conduit 31 in the direction of the microwave applicator 34. During the crossing of the zone of the conduit 31 surrounded by the applicator 34, the materials undergo irradiation with microwaves such that at the exit from the irradiated area the materials are in the desired dissection state. In the present application, it is desirable to have materials as dry as possible in order to reduce the volume of solid waste, and to facilitate their handling or subsequent packaging.
Le générateur à micro-ondes 35 et son applicateur 34 sont des dispositifs connus. On peut utiliser par exemple comme applicateur ceux décrits dans EP-0.252.542 ou tout autre système à section rectangulaire ou carrée formant cavité de traitement, conforme aux normes en vigueur, en particulier concernant les fuites micro-ondes. A ce propos, des capteurs de fuites micro-ondes sont prévus, d'une part, à proximité du générateur 35 et, d'autre part, dans l'habitacle où est installée la cuvette 1.The microwave generator 35 and its applicator 34 are known devices. One can use for example as an applicator those described in EP-0.252.542 or any other system with rectangular or square section forming a treatment cavity, in accordance with the standards in force, in particular concerning microwave leaks. In this connection, microwave leak sensors are provided, on the one hand, near the generator 35 and, on the other hand, in the passenger compartment where the bowl 1 is installed.
La fréquence du générateur micro-ondes est par exemple deThe frequency of the microwave generator is for example of
2450 MHz, ou une autre des fréquences autorisées pour l'application industrielle, scientifique ou médicale. Un ou plusieurs générateurs à puissance restituée de 800 , 1200 ou plusieur KW sont utilisés. De même, il peut être prévu plusieurs applicateurs 34. Un même applicateur peut être relié à plusieurs générateurs, de même que plusieurs ensembles générateur-appliσateur peuvent être placés en parallèle et côte à côte autour du conduit 31.2450 MHz, or another of the frequencies authorized for industrial, scientific or medical application. One or more generators with restored power of 800, 1200 or more KW are used. Likewise, several applicators 34 can be provided. The same applicator can be connected to several generators, just as several generator-applicator assemblies can be placed in parallel and side by side around the duct 31.
La puissance de l'unité de génération de micro-ondes est calculée de telle sorte qu'elle permette le degré de dessication désiré des matières traitées, le débit de ces dernières dans la zone du conduit 31 traversant le ou les applicateurs 34, déterminé et réglé par la vitesse de rotation de la vis 32, étant également un paramètre essentiel du traitement micro-ondes.The power of the microwave generation unit is calculated so that it allows the desired degree of drying of the treated materials, the flow rate of the latter in the zone of the conduit 31 passing through the applicator (s) 34, determined and regulated by the speed of rotation of the screw 32, also being an essential parameter of the microwave treatment.
Ces divers paramètres dépendent bien entendu du volume de déjections à traiter.These various parameters obviously depend on the volume of excrement to be treated.
Dans l'installation de la figure 1, les matières dessiquees sont acheminées par le conduit 8 par la poussée exercée par les matières sous-jacentes elles-mêmes poussées par la vis 32, en direction de l'extracteur 7 chargé de collecteur la vapeur d'eau engendrée au cours du traitement des matières.In the installation of FIG. 1, the desiccated materials are conveyed through the conduit 8 by the thrust exerted by the underlying materials themselves pushed by the screw 32, in the direction of the extractor 7 responsible for collecting the vapor d water generated during material processing.
Ensuite, les matières dessiquees sont poussées dans la cuve 9 où elles sont ensachées à la manière des poussières dans un sac d'aspirateur. Ainsi, les matières dessiquees sont enfermées dans un sac étanche facile à manipuler en vue de son évacuation ou d'un éventuel traitement de récupération ultérieure.Then, the desiccated materials are pushed into the tank 9 where they are bagged like dust in a vacuum cleaner bag. Thus, the desiccated materials are enclosed in a waterproof bag which is easy to handle with a view to its evacuation or a possible subsequent recovery treatment.
Dans le mode de réalisation simplifié de la figure 2, les matières dessiquees sont stockées dans le réservoir 38 et récupérées par l'intermédiaire d'une trappe de visite 45. Dans l'installation de la figure 1 l'unité 5 ne reçoit que les matières solides en provenance de la cuve 3. Sur la figureIn the simplified embodiment of FIG. 2, the desiccated materials are stored in the reservoir 38 and recovered by means of an inspection hatch 45. In the installation of FIG. 1, the unit 5 receives only the solids from tank 3. In the figure
3 on a représenté schématiquement un mode de réalisation d'une telle cuve.3 schematically shows an embodiment of such a tank.
Celle-ci est constituée d'une enceinte cylindrique 46 d'axe vertical, munie en son centre d'une trappe d'accès 47 permettant notamment la mise en place d'un filtre cylindrique central 48. L'espace annulaire interne de l'enceinte 46 est divisé en deux parties par une grille 49 de forme tronσonique délimitant un espace inférieur 50 de collecte de la partie liquide 51 (urine et eau) des déjections et un espace supérieurThis consists of a cylindrical enclosure 46 of vertical axis, provided in its center with an access hatch 47 allowing in particular the installation of a central cylindrical filter 48. The internal annular space of the enclosure 46 is divided into two parts by a grid 49 of tronσonic shape delimiting a lower space 50 for collecting the liquid part 51 (urine and water) droppings and a higher space
52 de collecte des parties solides.52 for collecting solid parts.
Les déjections (mélange solides/liquides) sont introduites dans l'enceinte 46 par un conduit (2 dans le mode de réalisation de la figure 1) ou par plusieurs si la même installation traite les déjections de plusieurs cuvettes 1 reliées à la même cuve 3.The droppings (solid / liquid mixture) are introduced into the enclosure 46 by a conduit (2 in the embodiment of FIG. 1) or by several if the same installation treats the droppings from several bowls 1 connected to the same tank 3 .
La partie liquide 51 est évacuée par le conduit 23 relié à ladite cuve d'évaporation 25.The liquid part 51 is evacuated through the conduit 23 connected to said evaporation tank 25.
La partie solide 53 est dirigée par le conduit 4 à l'unité de traitement (5,6). Il est à noter que l'inclinaison de la grille 49 a tendance à pousser par un effet de coin les matières solides 53 vers l'extérieur, en direction de l'orifice du conduit 4.The solid part 53 is directed through the conduit 4 to the processing unit (5,6). It should be noted that the inclination of the grid 49 tends to push the solid materials 53 outwards towards the orifice of the duct 4 by a wedge effect.
La cuve d'évaporation 25, dont la structure et le fonctionnement sont bien connus, permet de récupérer l'eau par condensation de la vapeur amenée par la canalisation 28 dans la cuve de condensation 11.The evaporation tank 25, the structure and operation of which are well known, makes it possible to recover the water by condensation of the steam supplied by the pipe 28 into the condensation tank 11.
L'eau ainsi récupérée est avantageusement recyclée vers la cuvette 1 par exemple, ce qui permet de faire fonctionner l'installation de manière autonome sans nécessité de la relier à un réseau extérieur de fourniture d'eau.The water thus recovered is advantageously recycled to the bowl 1 for example, which makes it possible to operate the installation independently without the need to connect it to an external water supply network.
Eventuellement, un simple réservoir d'eau d'appoint (non représenté) peut être prévu dans l'installation.Optionally, a simple make-up water tank (not shown) can be provided in the installation.
Alors que dans le mode de réalisation de la figure 1, seules les matières solides sont envoyées vers la vis d'acheminement 32, dans le mode de réalisation de la figure 2, c'est l'ensemble solides/liquides qui est admis directement, par la canalisation 2, dans le logement de la vis 32.While in the embodiment of FIG. 1, only the solid materials are sent to the conveying screw 32, in the embodiment of FIG. 2, it is the solid / liquid assembly which is admitted directly, by line 2, in the housing of screw 32.
L'évacuation de la partie liquide se fait par gravité à l'extrémité inférieure du conduit 31, par la canalisation 41.The liquid part is evacuated by gravity at the lower end of the duct 31, via the pipe 41.
D'une manière générale, la vis 32 est mise en service automatiquement grâce à un capteur de présence de matière disposé à proximité du débouché du conduit (4, figure 1 ; 2, figure 2) d'introduction des matières à traiter dans le logement de la vis 32, un tel capteur étant symbolisé en 54 sur la figure 2 et relié (55) à l'ensemble moto-réducteur 33In general, the screw 32 is automatically put into service thanks to a material presence sensor disposed near the outlet of the conduit (4, Figure 1; 2, Figure 2) for introducing the materials to be treated into the housing. of screw 32, such a sensor being symbolized at 54 on Figure 2 and connected (55) to the gear motor assembly 33
(36,37) de commande de la vis. Un tel capteur 54 peut être placé dans la cuve 3 (figure 3) en un endroit approprié.(36,37) for controlling the screw. Such a sensor 54 can be placed in the tank 3 (FIG. 3) at a suitable location.
Si seules les matières solides sont à envoyer dans le module d'acheminement 5, les matières liquides peuvent être séparées avant introduction dans le module 5 par tous moyens appropriés, avec récupération et recyclage de l'eau ou simple élimination.If only the solid materials are to be sent into the routing module 5, the liquid materials can be separated before introduction into the module 5 by any appropriate means, with recovery and recycling of the water or simple elimination.
Il est à noter qu'une telle séparation n'est pas indispensable, le mélange solides/liquides pouvant être traité sans séparation dans l'unité 6, le ou les générateurs de micro¬ ondes étant réglés en conséquence, les vapeurs d'eau recueillies par l'extracteur 7 et complémentairement par l'enceinte 9 étant simplement plus importantes en quantité. L'eau de condensation est soit récupérée et recyclée, soit éliminée par tous moyens appropriés.It should be noted that such separation is not essential, the solid / liquid mixture can be treated without separation in unit 6, the microwave generator (s) being adjusted accordingly, the water vapors collected by the extractor 7 and additionally by the enclosure 9 being simply greater in quantity. The condensed water is either recovered and recycled, or eliminated by any appropriate means.
Dans les modes de réalisation des figures 1 et 2, la vis 32 est disposée à la verticale mais elle pourrait être agencée différemment et être, par exemple, inclinée ou à l'horizontale.- La figure 4 illustre une variante d'application du procédé de l'invention au traitement de grandes quantités de déjections et tout particulièrement de déjections animales.In the embodiments of FIGS. 1 and 2, the screw 32 is arranged vertically but it could be arranged differently and be, for example, inclined or horizontal. FIG. 4 illustrates a variant application of the method of the invention to the treatment of large quantities of excrement and very particularly of animal excrement.
La figure 4 représente schématiquement une installation de traitement en cascade comprenant une trémie 56 de réception des matières (solides et liquides mélangés) à traiter, une trémie 57 de réception des matières dessiquees après traitements aux micro-ondes opérés dans une pluralité d'unités en série 58a, 58b, etc.. en nombre variable.FIG. 4 schematically represents a cascade treatment installation comprising a hopper 56 for receiving the materials (solids and mixed liquids) to be treated, a hopper 57 for receiving the desiccated materials after microwave treatments operated in a plurality of units in series 58a, 58b, etc. in variable number.
Chaque unité 58a, 58b, etc... , comprend au moins un conduit d'acheminement horizontal 59 muni par exemple d'une vis d'Archimède analogue à celle du dispositif de la figure 2, entraînée par un moto-réducteur 60. Chaque conduit 59 relie une trémie amont à une trémie aval. Sur la figure 4 sont représentées, outre les deux trémies d'extrémité 56,57, deux trémies intermédiaires 61 et 62 respectivement.Each unit 58a, 58b, etc., comprises at least one horizontal conveying conduit 59 provided for example with an Archimedes screw similar to that of the device in FIG. 2, driven by a geared motor 60. Each conduit 59 connects an upstream hopper to a downstream hopper. In Figure 4 are shown, in addition to the two end hoppers 56, 57, two intermediate hoppers 61 and 62 respectively.
Chaque conduit 59 est équipé d'au moins un ensemble générateur-appliσateur de micro-ondes 63 et d'au moins un extracteur de vapeurs 64 entourant le conduit 59 qui est, à ce niveau, muni de perforations ou analogues dans sa paroi pour l'extraction des vapeurs. Les extracteurs 64 sont reliés par des conduits 65 à une unité (non représentée) de condensation pour la récupération et l'éventuel recyclage de l'eau extraite des matières traitées.Each duct 59 is equipped with at least one generator-microwave appliσator 63 and at least one vapor extractor 64 surrounding the duct 59 which is, at this level, provided with perforations or the like in its wall for the extraction of vapors. The extractors 64 are connected by conduits 65 to a condensing unit (not shown) for the recovery and possible recycling of the water extracted from the treated materials.
Dans le schéma de la figure 4, chaque unité 58a,58b,etc... comporte un seul conduit 59, un seul ensemble générateur- applicateur 63 et un seul extracteur 64, mais on peut prévoir un seul conduit 59 et plusieurs dispositifs 63 et 64 côte à côte, ou bien plusieurs conduits 59 en parallèle avec chacun un ou plusieurs dispositifs 63 et un ou plusieurs dispositifs 64. Le dispositif extracteur 64 peut être constitué par exemple par une chambre d'application de micro-ondes du type équipant le dispositif 63 et dont l'entrée, au lieu d'être raccordée à un générateur micro-ondes serait reliée au conduit d'extraction 65, le conduit 59 étant bien entendu muni de perforations ou passages dans sa paroi à hauteur de cette chambre d'application.In the diagram of FIG. 4, each unit 58a, 58b, etc ... comprises a single conduit 59, a single generator-applicator assembly 63 and a single extractor 64, but one can provide a single conduit 59 and several devices 63 and 64 side by side, or else several conduits 59 in parallel with each one or more devices 63 and one or more devices 64. The extractor device 64 can be constituted for example by a microwave application chamber of the type equipping the device 63 and whose inlet, instead of being connected to a microwave generator, would be connected to the extraction duct 65, the duct 59 being of course provided with perforations or passages in its wall at the level of this application chamber .
Chaque trémie intermédiaire 61,62 comporte, en partie haute, un orifice de déversement du conduit 59 de l'unité de traitement amont et, en partie basse, la vis d'acheminement de l'unité de traitement aval.Each intermediate hopper 61, 62 has, in the upper part, a discharge orifice for the conduit 59 of the upstream processing unit and, in the lower part, the conveying screw of the downstream processing unit.
De plus, chaque trémie intermédiaire 61,62 est coiffée d'un collecteur 66 d'extraction des vapeurs également relié à ladite unité de condensation.In addition, each intermediate hopper 61, 62 is capped with a vapor extraction manifold 66 also connected to said condensing unit.
Les paramètres des unités de traitement 58a,58b,etσ... , à savoir fréquence des micro-ondes, débit des matières dans le ou les conduits 59, sont réglés de façon que la matière déversée dans la trémie finale 57 ait le degré de dessication désiré, les degrés de dessication des matières dans les trémies intermédiaires 61,62 étant intermédiaires entre celles des états respectivement initiaux et finaux des matières traitées.The parameters of the processing units 58a, 58b, etσ ..., namely frequency of the microwaves, flow of materials in the conduit (s) 59, are adjusted so that the material discharged into the final hopper 57 has the degree of desired desiccation, the degrees of desiccation of the materials in the intermediate hoppers 61, 62 being intermediate between those of the respectively initial and final states of the materials treated.
Une telle installation permet le traitement de quantités importantes de déjections notamment d'origine animale.Such an installation allows the treatment of large quantities of excrement, notably of animal origin.
Les matières dessiquees se trouvent en vrac dans la ou les trémies 57 et sont évacuées par tous moyens appropriés à des fins d'élimination, retraitement ou recyclage.The desiccated materials are in bulk in the hopper (s) 57 and are evacuated by any appropriate means for the purpose of elimination, reprocessing or recycling.
Par ailleurs, sans sortir du cadre de l'invention, on peut imaginer tout autre moyen qu'une vis d'Archimède pour acheminer dans les conditions requises de débit contrôlé les matières à traiter dans l'espace d'application des micro-ondes, lequel espace peut avoir une configuration géométrique différente selon la nature du moyen d'acheminement et la morphologie du conduit d'acheminement des matières.Furthermore, without departing from the scope of the invention, it is possible to imagine any other means than an Archimedes' screw for conveying, under the conditions of controlled flow, the materials to be treated into the microwave application space, which space can have a different geometric configuration according to the nature of the conveying means and the morphology of the material conveying conduit.
Enfin, la séparation solides/gaz en aval du traitement aux micro-ondes peut s'opérer d'une autre manière que par extraction de vapeur et condensation de l'eau à la pression atmosphérique, à la manière connue, comme c'est le cas dans l'installation de la figure 1. Finally, the solid / gas separation downstream of the microwave treatment can be carried out in another way than by steam extraction and condensation of water at atmospheric pressure, in the known manner, as is the case. case in the installation of figure 1.

Claims

11R E V E N D I C A T I O N S 11R EVENDICATIONS
1. Procédé de traitement des déjections humaines ou animales par micro-ondes, caractérisé en ce qu'il consiste à soumettre au moins les parties solides des déjections à traiter à une irradiation par micro-ondes dans des conditions contrôlées en sorte qu'en fin de traitement desdites parties celles-ci aient atteint un degré de dessication prédéterminé.1. Process for treating human or animal excrement by microwave, characterized in that it consists in subjecting at least the solid parts of the excrement to be treated to irradiation by microwave under controlled conditions so that at the end treatment of said parts they have reached a predetermined degree of desiccation.
2. Procédé suivant la revendication 1, caractérisé en ce que les déjections à traiter, à savoir les parties solides seules ou en mélange avec les parties liquides, sont contraintes de défiler dans un espace déterminé soumis aux irradiations micro-ondes, dans des conditions de débit déterminées de façon à obtenir le degré désiré de dessication des matières traitées à la sortie de la zone d'irradiation.2. Method according to claim 1, characterized in that the droppings to be treated, namely the solid parts alone or in admixture with the liquid parts, are forced to pass through a determined space subjected to microwave irradiation, under conditions of flow rates determined so as to obtain the desired degree of desiccation of the materials treated at the outlet of the irradiation zone.
3. Procédé suivant l'une des revendications 1 ou 2, caractérisé en ce qu'on recueille la vapeur d'eau dégagée au cours du traitement aux micro-ondes en vue d'un éventuel recyclage ou récupération de l'eau de condensation.3. Method according to one of claims 1 or 2, characterized in that the water vapor released during the microwave treatment is collected with a view to possible recycling or recovery of the water of condensation.
4. Procédé suivant l'une des revendications 1 à 3, caractérisé en ce qu'on recueille lesdites matières dessiquees et on les conditionne en vue de leur élimination ou d'un traitement ultérieur.4. Method according to one of claims 1 to 3, characterized in that said desiccated materials are collected and conditioned for their elimination or subsequent treatment.
5. Procédé suivant l'une des revendications 1 à 4, caractérisé en ce que seules les parties solides sont traitées aux micro-ondes, les parties liquides étant séparées avant le traitement et soumises à évaporation pour recueillir l'eau en vue de son éventuel recyclage ou récupération.5. Method according to one of claims 1 to 4, characterized in that only the solid parts are treated in the microwave, the liquid parts being separated before the treatment and subjected to evaporation to collect the water with a view to its possible recycling or recovery.
6. Dispositif pour la mise en oeuvre du procédé selon l'une des revendications 2 à 5, caractérisé en ce qu'il comporte des moyens (34,35) pour engendrer et appliquer des micro-ondes dans un espace confiné déterminé, disposé sur la trajectoire de déplacement des matières à traiter et des moyens (31,32) pour déplacer lesdites matières suivant ladite trajectoire à un débit contrôlé réglable et de façon à irradier la totalité des matières. 6. Device for implementing the method according to one of claims 2 to 5, characterized in that it comprises means (34,35) for generating and applying microwaves in a determined confined space, arranged on the path of movement of the materials to be treated and means (31,32) for moving said materials along said path at a controlled adjustable rate and so as to irradiate all of the materials.
7. Dispositif suivant la revendication 6, caractérisé en ce que lesdits moyens pour engendrer et appliquer les micro¬ ondes sont constitués par au moins un générateur de micro-ondes 127. Device according to claim 6, characterized in that said means for generating and applying microwaves consist of at least one microwave generator 12
(35) associé a au moins un applicateur de micro-ondes (34) entourant un conduit (31) dans lequel circule les matières à traiter, ledit conduit étant, au moins au niveau dudit applicateur, transparent vis à vis des micro-ondes. (35) associated with at least one microwave applicator (34) surrounding a conduit (31) in which the materials to be treated circulate, said conduit being, at least at the level of said applicator, transparent with respect to microwaves.
8. Dispositif suivant la revendication 7, caractérisé en ce que ledit conduit (31), en amont dudit applicateur de micro¬ ondes (34), est muni d'une vis transporteuse (32) mue par des moyens moteurs appropriés (33 ; 36,37), les matières à traiter étant acheminer dans le logement (31) de la vis (32), dans la zone amont de celle-ci, par au moins une canalisation (2;4).8. Device according to claim 7, characterized in that said conduit (31), upstream of said microwave applicator (34), is provided with a conveyor screw (32) moved by suitable motor means (33; 36 , 37), the materials to be treated being conveyed into the housing (31) of the screw (32), in the upstream region thereof, by at least one pipe (2; 4).
9. Dispositif suivant l'une des revendications 6 à 8, caractérisé en ce que les matières, immédiatement en sortie de l'espace d'irradiation, passent dans un extracteur de vapeurs (7) relié à une cuve de condensation (11) mise à l'atmosphère par une cheminée (12) munie d'un filtre.9. Device according to one of claims 6 to 8, characterized in that the materials, immediately out of the irradiation space, pass through a vapor extractor (7) connected to a condensation tank (11) put to the atmosphere by a chimney (12) fitted with a filter.
10. Dispositif suivant la revendication 9, caractérisé en ce qu'à la sortie dudit extracteur de vapeurs (7), les matières dessiquees sont recueillies et ensachées dans une enceinte fermée (9) munie d'une trappe d'accès (15) et d'une- canalisation (16) de récupération des gaz reliée à ladite cuve de condensation (11).10. Device according to claim 9, characterized in that at the outlet of said vapor extractor (7), the desiccated materials are collected and bagged in a closed enclosure (9) provided with an access hatch (15) and of a gas recovery pipe (16) connected to said condensation tank (11).
11. Dispositif suivant la revendication 9 ou 10, caractérisé en ce que la cuve de condensation (11) est munie d'un circuit (17 à 19) de récupération et recyclage de l'eau de condensation.11. Device according to claim 9 or 10, characterized in that the condensation tank (11) is provided with a circuit (17 to 19) for recovering and recycling the condensation water.
12. Dispositif suivant l'une des revendications 6 à 11, caractérisé en ce qu'il comporte une cuve (3) de séparation solides/liquides reliée, d'une part, à une ou plusieurs sources (1) de déjections à traiter, d'autre part, auxdits moyens (5,6; 31 à 35) d'acheminement et traitement aux micro-ondes des matières solides et, enfin, à un circuit d'évacuation ou traitement des matières liquides (23-25).12. Device according to one of claims 6 to 11, characterized in that it comprises a tank (3) of solid / liquid separation connected, on the one hand, to one or more sources (1) of manure to be treated, on the other hand, to said means (5,6; 31 to 35) for transporting and treating solids in the microwave and, finally, to a circuit for removing or treating liquids (23-25).
13. Dispositif suivant la revendication 12, caractérisé en ce que ladite cuve (3) de séparation solides/liquides est constituée d'une enceinte cylindrique d'axe vertical (46) munie d'un filtre central (48), d'une grille (49) de séparation solides/liquides de forme tronconique, coaxiale à ladite enceinte (46), d'au moins un orifice d'évacuation (23) des liquides, disposé en dessus de ladite grille, d'au moins un orifice d'évacuation (4) des solides, disposé au dessus de ladite grille et d'au moins un orifice d'introduction (2) des matières solides et liquides à traiter, disposé également au dessus de ladite grille.13. Device according to claim 12, characterized in that said tank (3) of solid / liquid separation consists of a cylindrical enclosure of vertical axis (46) provided with a central filter (48), a grid (49) separation of solids / liquids in frustoconical shape, coaxial with said enclosure (46), of at least one liquid evacuation orifice (23), disposed above said grid, of at least one orifice of evacuation (4) of solids, arranged above said grid and at least one introduction orifice (2) for the solid and liquid materials to be treated, also arranged above said grid.
14. Dispositif suivant la revendication 12 ou 13, caractérisé en ce que le circuit d'évacuation des liquides comporte une cuve d'évaporation (25) munie d'un circuit (28) de récupération de vapeur d'eau relié à ladite cuve de condensation (11) .14. Device according to claim 12 or 13, characterized in that the liquid evacuation circuit comprises an evaporation tank (25) provided with a circuit (28) for recovering water vapor connected to said tank. condensation (11).
15. Dispositif suivant la revendication 6, plus particu- lierement destiné au traitement de grandes quantités de déjections, caractérisé en ce qu'il comporte une trémie (56) d'introduction des matières à traiter, une trémie (57) de réception de matières dessiquees, une pluralité de trémies intermédiaires (61,62) et une pluralité d'unités de traitement micro-ondes en série (58a,58b), chaque unité comprenant au moins un conduit d'acheminement (59) avec ses moyens d'acheminement (60), au moins un ensemble générateur- applicateur de micro-ondes (63) et au moins un extracteur de vapeurs (64) et chaque trémie intermédiaire (61,62) étant munie d'un collecteur de vapeurs (66). 15. Device according to claim 6, more particularly intended for the treatment of large quantities of excrement, characterized in that it comprises a hopper (56) for introducing the materials to be treated, a hopper (57) for receiving materials desiccated, a plurality of intermediate hoppers (61,62) and a plurality of microwave processing units in series (58a, 58b), each unit comprising at least one conveying duct (59) with its conveying means (60), at least one generator-microwave applicator assembly (63) and at least one vapor extractor (64) and each intermediate hopper (61,62) being provided with a vapor collector (66).
EP90905203A 1989-03-09 1990-03-09 Devices for treating human or animal dejections by means of micro-waves Expired - Lifetime EP0413813B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT90905203T ATE96486T1 (en) 1989-03-09 1990-03-09 ARRANGEMENTS FOR MICROWAVE TREATMENT OF HUMAN OR ANIMAL WASTE.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8903267A FR2644154B1 (en) 1989-03-09 1989-03-09 DEVICE FOR PROCESSING HUMAN OR ANIMAL DEJECTIONS BY MICROWAVE ELECTRICAL SYSTEM, AND MECHANICAL TRANSFER SYSTEM
FR8903267 1989-03-09

Publications (2)

Publication Number Publication Date
EP0413813A1 true EP0413813A1 (en) 1991-02-27
EP0413813B1 EP0413813B1 (en) 1993-10-27

Family

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EP90905203A Expired - Lifetime EP0413813B1 (en) 1989-03-09 1990-03-09 Devices for treating human or animal dejections by means of micro-waves

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US (1) US5145576A (en)
EP (1) EP0413813B1 (en)
JP (1) JPH03504466A (en)
CA (1) CA2028099A1 (en)
DE (1) DE69004189T2 (en)
ES (1) ES2049028T3 (en)
FR (1) FR2644154B1 (en)
OA (1) OA09630A (en)
WO (1) WO1990010760A1 (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5447630A (en) * 1993-04-28 1995-09-05 Rummler; John M. Materials treatment process and apparatus
EP0846207A1 (en) * 1994-08-05 1998-06-10 Lykke Olesen Apparatus at a toilet
US5853579A (en) * 1996-11-26 1998-12-29 Wastech International Inc. Treatment system
US5958252A (en) * 1997-07-05 1999-09-28 Microseptic, Inc. Waste treatment device and method employing the same
US6139744A (en) * 1997-07-05 2000-10-31 Microseptec, Inc. Waste treatment device and method employing the same
CN1316361A (en) * 2000-02-02 2001-10-10 曾德邻 Collecting method, storage facilities and transporter of excrement and urine
CA2423581A1 (en) * 2003-03-27 2004-09-27 Brs Agri2000 Ltd. System and method for converting a biosolid sludge to a pasteurised stage for use as an organic fertilizer
US7360655B2 (en) * 2003-11-10 2008-04-22 Thor Global Enterprises Ltd. Material handling system having a scoop wheel
US7449107B2 (en) * 2004-10-29 2008-11-11 Steven Lumbert Dehydration toilet having an infusion odor capturing steam and water recovery system
US7211187B2 (en) * 2004-10-29 2007-05-01 Steven Lumbert Mobile or stationary modular self-contained dehydration toilet, dehydration engine, and gray water recovery system
WO2012009859A1 (en) * 2010-07-23 2012-01-26 Lam Kwok Fai Microwave dryer and microwave drying method
CN108218178B (en) * 2017-12-29 2020-12-18 嘉兴科禾能源科技有限公司 Portable livestock-raising farm excrement and urine automatic collection encapsulation equipment
CN111156792A (en) * 2020-01-20 2020-05-15 广州福滔微波设备有限公司 Tunnel type microwave drying equipment
CN116067161A (en) * 2023-01-09 2023-05-05 中车山东机车车辆有限公司济南低碳科技分公司 Drying feeding device

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3523076A (en) * 1968-07-30 1970-08-04 Bechtel Int Corp Microwave irradiation of sewage and sewage sludge
US3522613A (en) * 1968-10-21 1970-08-04 Samuel Botsford Waste disposal system
US3700565A (en) * 1970-04-03 1972-10-24 Koehler Dayton Microwave sewage system with distillation means
DE2021142A1 (en) * 1970-04-30 1971-11-18 Villeroy & Boch Toilet, in particular vehicle toilet
US3831288A (en) * 1970-11-24 1974-08-27 Furnace L Dev Ltd Drying and sterilising apparatus
US3655048A (en) * 1971-01-08 1972-04-11 Nicola F Pergola Method and apparatus for treating and disposing of sewage
US3868731A (en) * 1972-11-15 1975-03-04 Oliver B Stahl Closed cycle waste treatment system and method
US3882552A (en) * 1973-05-02 1975-05-13 Westinghouse Electric Corp Self-contained waste treatment system
US4193869A (en) * 1974-11-21 1980-03-18 Milton Brucker Wastewater and wastewater solid processing system
US4219415A (en) * 1978-08-09 1980-08-26 Nassef N A Method and apparatus for disposal of organic wastes
JPS571838Y2 (en) * 1978-11-21 1982-01-12
US4631133A (en) * 1984-09-13 1986-12-23 Axelrod R & D, Inc. Waste treatment device and method using microwaves
DE3505570C1 (en) * 1985-02-18 1991-01-24 GVB SANIMED Hygiene- und Medizintechnik GmbH, 3070 Nienburg Device for the treatment of infectious waste by means of microwaves
FR2599924B1 (en) * 1986-06-06 1988-09-09 Univ Bordeaux 1 MODULAR DEVICE FOR APPLYING MICROWAVE FOR THE HEATING, DRYING OR ROASTING OF A MATERIAL
US5037560A (en) * 1990-03-09 1991-08-06 Danny Gayman Sludge treatment process

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9010760A1 *

Also Published As

Publication number Publication date
JPH03504466A (en) 1991-10-03
DE69004189D1 (en) 1993-12-02
FR2644154B1 (en) 1991-06-14
CA2028099A1 (en) 1990-09-10
EP0413813B1 (en) 1993-10-27
WO1990010760A1 (en) 1990-09-20
DE69004189T2 (en) 1994-05-19
ES2049028T3 (en) 1994-04-01
US5145576A (en) 1992-09-08
FR2644154A1 (en) 1990-09-14
OA09630A (en) 1993-04-30

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