Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
  • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
  • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
  • B09B3/0075—Disposal of medical waste
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L11/00—Methods specially adapted for refuse
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
  • A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
  • A61L2/04—Heat
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
  • A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
  • A61L2/08—Radiation
  • A61L2/12—Microwaves
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
  • A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
  • A61L2/20—Gaseous substances, e.g. vapours
  • A61L2/202—Ozone
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
  • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
  • B02C19/00—Other disintegrating devices or methods
  • B02C19/0056—Other disintegrating devices or methods specially adapted for specific materials not otherwise provided for
  • B02C19/0075—Other disintegrating devices or methods specially adapted for specific materials not otherwise provided for specially adapted for disintegrating medical waste
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
  • A61L2202/10—Apparatus features
  • A61L2202/12—Apparatus for isolating biocidal substances from the environment
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
  • A61L2202/10—Apparatus features
  • A61L2202/12—Apparatus for isolating biocidal substances from the environment
  • A61L2202/121—Sealings, e.g. doors, covers, valves, sluices
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
  • A61L2202/10—Apparatus features
  • A61L2202/16—Mobile applications, e.g. portable devices, trailers, devices mounted on vehicles

Definitions

• the present invention relates to the field of waste, and particularly waste from care activities with infectious risks (DASRI). It finds a particularly advantageous application in the field of the trivialization of DASRI.
• DASRI commoditization systems There are a large number of DASRI commoditization systems in the prior art. Usually these systems include a waste grinding device and a waste heating device, and often the two devices form only one for heating during grinding, for example.
• document WO2013110900 A1 which describes a DASRI commodity system comprising a tank mounted on a frame, grinding means mounted at the bottom of the tank and a device for heating the waste with a view to their disinfection.
• This heating device comprises a microwave generator connected by a waveguide to the tank, the waste thus being heated in the tank where they are crushed.
• the heating is generated by microwaves and the waste is heated in the grinding tank.
• An object of the present invention is therefore to provide a solution to this problem.
• patent publication WO 2013/096782 A2 discloses a medical waste treatment system.
• the technique presented includes a waste transport line.
• the management of this line in particular of the atmosphere of its enclosure, is not optimal.
• a system for the trivialization of waste, in particular waste from healthcare activities with infectious risks characterized in that it comprises: a. a transport line configured to circulate the waste between an inlet zone and an evacuation zone of the system, and comprising a conveying device, the conveying device being configured to circulate the waste over at least part of the transmission line, b.
• a heater configured to heat at least part of the waste as the waste travels over at least part of the transport line
• the system comprises a tunnel sealing at least part of the transport line of waste, the conveyor device being housed in said tunnel, said tunnel comprising a waste inlet and a waste outlet, and in that the system further comprises an ozone injection device configured to apply ozone on at least part of the waste when the waste circulates on at least part of the transport line.
• the present invention makes it possible to disinfect at least some of the elements making up the system, in particular the tunnel. It allows a user to work in safety during repairs, for example.
• ozone allows disinfection of the various areas where it circulates in the system. It can be used to disinfect, for example, the crusher, or the feed hopper, or the tunnel effectively and during use of the system.
• ozone can disinfect the entire tunnel.
• the present invention makes it possible to disinfect the tunnel, for example by continuing the injection of ozone to disinfect the entire tunnel and allow a user to carry out maintenance operations in complete safety if necessary.
• the present solution allows to reduce or even eliminate odors by the oxidizing power of ozone, which allows easier integration of the equipment. Finally, it makes it possible to eliminate, at least in part, the aero-contaminants which represent a significant risk of contamination during the grinding of the bins / bags of infectious hospital waste, for example.
• the present solution synergistically combines heat and ozone in order to have a complementary disinfection of the waste.
• Ozone has a disinfectant power of surface and penetrates inside the waste according to its texture, and the heat allows the waste to rise in temperature and disinfection.
• Another aspect relates to a method of trivializing waste, in particular waste from healthcare activities with infectious risks, comprising at least the following steps implemented by the system according to the present solution: a. Circulation of waste in a tunnel by a conveyor device on a transport line, the tunnel sealingly closing at least part of the waste transport line; b. Heating of the waste circulating in the tunnel by at least one heating device; vs. Before or during the two previous steps, application of ozone to at least part of the waste circulating along the transport line by an ozone injection device.
• FIG. 1 schematically represents a commodity system according to an embodiment of the present invention.
• the system comprises at least one extraction device configured to extract, from a first zone of the tunnel, at least a portion of the atmosphere contained in the tunnel.
• the extraction device is configured to analyze at least one parameter of the atmosphere taken from at least: hydrometry, temperature, ozone concentration.
• the extraction device is configured to at least partially reinject said portion of atmosphere from a second zone of the tunnel. This allows the waste to be preheated and at least part of the ozone injected to be reused. This makes it possible to reduce the heating power required to reach a predetermined disinfection temperature.
• the portion extracted from the atmosphere is a gas mixture comprising at least part of the ozone injected by the injection device and at least one other gas.
• the first zone is located at the level of the exit of the tunnel and the second zone is located at the level of the entrance of the tunnel.
• the system comprises at least one waste mixing device arranged upstream of the entrance to the tunnel in a direction of transport of the waste passing through the inlet and then through the outlet.
• the stirring device is a waste grinding device.
• ozone is injected into the mixing device and / or upstream of the mixing device in a direction of transport of the waste passing through the inlet and then through the outlet.
• the system comprises at least one feed hopper arranged upstream of the stirring device in a direction of transport of the waste passing through the inlet and then through the outlet, and the injection device is configured to inject the ozone at the feed hopper.
• the injection device is configured to inject ozone at the waste intake area.
• the injection device is configured to inject ozone at the entrance to the tunnel.
• the transport line has a portion inclined relative to a horizontal plane so that part of this inclined portion is located at a height less than the height at which another part of this inclined portion is located. report to the horizontal plane.
• the conveying device is inclined relative to a horizontal plane in the direction of circulation of the waste.
• the conveyor device comprises at least a first conveyor and a second conveyor.
• the first conveyor and the second conveyor have a height offset H relative to each other so that the waste arriving at the end of the travel of the first conveyor falls on the second conveyor. ⁇ This allows a stirring effect of the wastes in the tunnel in order to change their orientation with respect to the ozone and also to the heater.
• the system includes at least one sensor configured to measure the concentration of ozone in the atmosphere outside the tunnel.
• the system comprises at least one sensor configured to measure the concentration of ozone in the tunnel and preferably the rate of hydrometry.
• the ozone injection device is configured so that the concentration of ozone in the tunnel is at least equal to a few grams per m3.
• the heating device comprises at least one microwave generator. According to one example, the heating device comprises a plurality of microwave generators.
• the heating device comprises at least a plurality of microwave generators with associated waveguides for transmitting the microwaves generated by the microwave generator into the tunnel.
• the heating device comprises at least a plurality of microwave generators and a plurality of waveguides configured to transmit in the tunnel the microwaves generated by the microwave generator, preferably each waveguide. waves of the plurality of waveguides being associated with a microwave generator of the plurality of microwave generators.
• the heater comprises at least a plurality of microwave generators and a plurality of associated waveguides configured so that the generated microwaves are distributed along the transmission line in the tunnel.
• the microwave heater is configured so that the generated microwaves are distributed along the transport line in the tunnel.
• microwaves have a core disinfecting power to radiate from the center of the waste to the outside. This makes it possible to heat the waste all along the tunnel and in a homogeneous manner.
• the ozone application step is carried out before and / or at the same time as the heating step.
• ozone has a surface disinfectant power.
• the method comprises, before the circulation step, a stirring step, preferably of crushing of the waste, by a stirring device, preferably by a crushing device.
• the method comprises at least one step of extracting, from a first zone of the tunnel, at least a portion of the atmosphere contained in the tunnel.
• the method comprises, after the extraction step, at least one reinjection step from a second zone of the tunnel of said portion taken from the atmosphere.
• the second zone of the tunnel comprises at least one airlock, preferably comprising at least one intermediate hopper, and the extraction device is configured to at least partially reinject said portion of atmosphere into said airlock.
• the field of application of the present invention is the trivialization of waste and in particular waste from care activities with infectious risks (DASRI).
• DASRI infectious risks
• the present invention allows the treatment of a large amount of waste, and preferably in the chain, and advantageously continuously.
• the present invention further allows disinfection of waste but also of at least part of the commodity system, simply, quickly and reliably.
• the waste commodity system 100 comprises: a. A transport line 101 of waste 10; b. Preferably, a heater 120; vs. A tunnel 130 hermetically closing at least part of the transport line 101; d. An ozone injection device 140; e. Preferably, an extraction device 150; f. Preferably, a brewing device 160.
• the waste transport line 101 is configured to circulate the waste 10 through the system 100 for commuting.
• the waste transport line 101 10 is configured to circulate the waste 10 between an inlet area 102 and an outlet area 103 of the system 100 according to the present invention.
• Part of the transport can be sequential, for example by moving the waste in successive batches. This may be the case during grinding, for example.
• Another part of line 101 can move continuously. This may be the case during a conveying operation.
• This transport line 101 can preferably include a device 110 for conveying the waste 10.
• the conveying device 110 is configured to circulate the waste 10 over at least part of the transport line 101.
• the conveying device can comprise one or more conveyors.
• a conveyor could comprise a belt on the upper surface of which the waste is placed in transit, and means for driving the belt, for example in the form of rollers; the carpet forms a continuous whole, rotating in a loop.
• the conveying device 110 comprises a first conveyor 111 and a second conveyor 112.
• These conveyors 111 and 112 may be of the same type or have a different conveying mechanism.
• the first conveyor 111 and the second conveyor 112 are arranged relative to each other so as to allow mixing of the waste, in particular a spatial repositioning of the waste 10. This thus makes it possible to stir the waste 10 and improve their focus contact with the atmosphere 133 of the tunnel 130 and therefore with the ozone. This also makes it possible to improve the homogeneity of the heating of the waste 10 as it circulates in the tunnel 130.
• the first conveyor 111 and the second conveyor 112 can be arranged relative to each other so that when the waste 10 reaches the end of the travel of the first conveyor 111, they fall on the second conveyor 112, this drop allowing the stirring of the waste 10.
• the end of the first conveyor 111 can be placed in line with the start of the second conveyor 112, for example, preferably in a dimension in height H greater at 20cm, preferably at 50cm.
• the first conveyor 111 unloads the waste onto the second conveyor 112, in order to provide a mixing function and to optimize the penetration of the waste. ozone and microwaves in the waste. This thus makes it possible to increase the effectiveness of trivialization.
• the first conveyor 111 and / or the second conveyor 112 can be inclined with respect to each other and / or with respect to the horizon.
• this inclination is configured so that the exit of the waste is lower in altitude than its entry on the conveying device.
• the inclination of the conveyors can be the same.
• the inclination relative to the horizontal should be chosen to be less than 10 °.
• the heating device 120 is configured to heat at least part of the waste 10 when the waste 10 circulates on at least part of the transport line 101, preferably in the tunnel 130.
• this heating device 120 can include one or more microwave generators, and / or include one or more waveguides.
• the heater 120 is configured to heat at least a portion of the waste 10 to a temperature above 100 ° C.
• At least part of the heating takes place during conveying. This does not exclude, in addition or alternatively, that the heating is produced at other places of the transport line 101, for example during grinding.
• the heating device 120 comprises a plurality of microwave generators 121 arranged along the tunnel 130 so as to allow homogeneous irradiation of at least part of the waste 10 passing through the tunnel 130. .
• the plurality of microwave generators 121 can be distributed at different locations around the conveying device 110 so as to radiate from the top and from the bottom, and / or on one side and on the other, the waste 10 during its transport in at least part of the tunnel 130.
• the waste tunnel 130 comprises an inlet 131 for waste 10 and an outlet 132 for waste 10.
• the conveying device 110 is housed in the tunnel 130.
• the first conveyor 111 is positioned from so as to directly receive the waste 10 entering, preferably falling, via the entrance 131 of the tunnel 130.
• the second conveyor 112 is positioned so as to evacuate, preferably drop, the waste 10 towards the outlet 132.
• this tunnel 130 defines an airtight volume around part of the transport line 101.
• the atmosphere 133 present in this volume is intended to be confined therein relatively to the outside of the tunnel 130.
• the ozone injection device 140 is configured to inject ozone into the atmosphere 133 of the tunnel 130, preferably to inject a predetermined quantity of ozone into the atmosphere 133 of the tunnel 130.
• the injection device 140 is configured to apply ozone, preferably a predetermined quantity of ozone, to at least part of the waste 10 when it is in the tunnel 130.
• the injection device 140 is configured to inject the ozone at the inlet 131 of the waste 10 in the tunnel 130.
• the expression “at” can be understood as “ inside of " ; for example, the injection of a gas at a device is understood to mean the injection of said gas into at least part of a volume defined by at least part of said device.
• the injection device 140 is configured to inject ozone into the first third of the length of the transport line 101 located in the tunnel 130, preferably in its first quarter.
• the injection device 140 can also inject ozone through an airlock 170 separating the admission zone 102 from the entrance 131 of the tunnel 130.
• the mixing device 160 is arranged upstream of the entrance 131 of the tunnel 130, for example before the airlock 170.
• the direction of transport of the waste is considered as passing through the entrance. 101 then by the exit 102 of the system.
• This stirring device 160 can for example be a grinder.
• This stirring device 160 is configured to stir, or even to grind, the waste 10.
• the stirring device 160 makes it possible to grind the waste 10 before it enters the tunnel 130.
• the ozone is injected at the level of the SAS 170, when the latter is closed, preferably by means of a cover for example, in order to disinfect the aero-contaminants generated during the brewing, preferably waste grinding.
• the ozone is injected downstream of the mixing device 160 as illustrated in FIG. 1.
• the airlock 170 can separate the mixing device 160 from the tunnel 130, and preferably from the place of injection of the ozone by the injection device 140.
• the airlock 170 may include a hatch opening onto the entrance 131 of the tunnel 130, or even forming at least part of said entrance 131 of the tunnel 130. This hatch is advantageously hermetic when it is closed.
• the airlock 170 comprises an intermediate hopper.
• the injection of ozone by the injection device 140 can be carried out at this intermediate hopper which makes it possible to inject, preferably continuously, ozone into the tunnel 130, and therefore to disinfect. , preferably continuously, the waste circulating in the tunnel 130.
• the injected ozone mixed with the atmosphere 133 of the tunnel 130 circulates in the tunnel 130 by means of the extraction device 150. Cleverly, as soon as the extraction is stopped, the injection of ozone stops automatically.
• the ozone is injected into a volume defined by at least part of the mixing device 160.
• the ozone is injected before or during the mixing of the waste 10.
• the stirring device comprises a tank, advantageously hermetic, intended to contain the waste 10 during their stirring. Said volume into which ozone is injected can be defined by this tank. This allows the waste 10 to be exposed to ozone directly in the brewer vessel 160, thereby disinfecting the interior of the vessel.
• a supply hopper 180 is disposed downstream of the brewing device 160.
• This supply hopper 180 comprises a hermetic hatch making it possible to make the interior of the brewing device 160 hermetic relative to the exterior.
• the injection device 140 can then be configured to inject the ozone into the feed hopper 180 so that the waste is in contact with the ozone at the time of their mixing, preferably grinding, by the stirring device 160.
• This allows the waste 10 in the feed hopper 180 to be disinfected before grinding, preferably at room temperature.
• This also makes it possible to disinfect the interior of the brewing device 160 and the feed hopper 180, preferably continuously, in particular before the opening of the airlock 170 of the tunnel 130.
• this makes it possible to eliminate the aero- contaminants in the brewing volume.
• the injection of ozone takes place only when the feed hopper 180 is closed, that is to say when its cover towards the outside is closed.
• the ozone is injected upstream of the mixing device 160.
• the feed hopper 180 includes a cover, preferably motorized.
• the device for injection 140 is configured to inject ozone at the feed hopper 180 only when the cover is closed.
• the ozone is injected both upstream and downstream of the stirring device 160, preferably at the level of the stirring device 160 and downstream of the stirring device 160.
• the ozone injection device 140 is configured to inject ozone at the level of the feed hopper 180, or even in the tank of the stirring device 160, before or while the waste is stirred, preferably crushed, and for injecting ozone at the level of the intermediate hopper, that is to say at the level of the airlock 170, in order to supply the atmosphere of tunnel 130 with ozone.
• the ozone injected into the intermediate hopper comes, at least in part, from the reinjection circuit 151.
• the system 100 is configured to receive ozone upstream and downstream of the mixing device 160.
• the extraction device 150 is configured to extract at least a portion of the atmosphere 133 from the tunnel 130.
• the extraction device 150 is configured to extract a gaseous mixture of ozone and water vapour.
• This water vapor preferably comes from heating the waste 10.
• at least part of the waste 10 produces water vapor.
• the waste 10 generates steam, which will then be extracted, at least in part, and reinjected at the level of the entrance 131 of the tunnel 130 to preheat this waste 10.
• This preheating facilitates the rise in temperature of the waste 10 circulating in the tunnel 130. This makes it possible to reduce the heating power required to obtain the disinfection of the waste 10.
• This water vapor and part of the ozone then form a hot gas mixture.
• this hot gas mixture preferably during the treatment of the waste, has a temperature above 70 ° C, preferably at 85 ° C and advantageously at 100 ° C.
• the extraction device 150 is also configured to allow the reinjection of said portion withdrawn from atmosphere 133 into the tunnel 130.
• the extraction device 150 is configured to extract said portion withdrawn at the level of a first zone 133 of the tunnel 130, preferably close to or coincident with the exit 132 of the tunnel 130.
• the extraction device 150 is configured to allow the reinjection of said portion withdrawn at the level of a second zone 134 of the tunnel 130, preferably close to or coincident with the entrance 131 of the tunnel 134, or even with the ozone injection zone.
• the reinjection of said withdrawn portion is carried out by the injection device 140.
• this reinjection circuit 151 which allows the hot gas mixture to circulate from the first zone 133 of the tunnel 130 to the second zone 134 of the tunnel 130. According to one embodiment, this reinjection circuit fluidly connects the extraction device 150 to the injection device 140.
• the extraction of this hot gas mixture at the level of the end of the tunnel 130 and its reinjection at the level of the start of the tunnel 130 makes it possible to preheat the waste 10 entering the tunnel 130 and thus makes it possible to reduce the heating power. required supplied by the heater 120.
• the reinjection of the hot gas mixture is done either at the level of the feed hopper, or at the level of the stirring device, or again at the level of the airlock 170, so as to preheat the waste 10.
• This therefore makes it possible to limit the heating power necessary for the heating device 120 to obtain the disinfection level, preferably equal to 100 ° C.
• the ozone injected beforehand thus mixes with this hot gas mixture comprising water vapor.
• the present invention allows, during the circulation of the waste 10 in the tunnel 130, to expose this waste 10 to a predetermined temperature and to a predetermined ozone level, so as to allow their trivialization as well as the disinfection of the environment. inside tunnel 130.
• the present invention also relates to a method of trivializing waste, in particular waste from healthcare activities with infectious risks.
• This method comprises at least the following steps: a. Preferably mixing of waste 10 by a mixing device 160 arranged upstream of the entrance 131 of the tunnel 130; b. Circulation of waste 10 in the tunnel 130 by the conveying device 110 along the transport line 101; vs. Preferably, heating of at least part of the waste 10 circulating in the tunnel 130 by the heating device 120; d. Before and / or during the previous steps, application of ozone to at least part of the waste 10 by the injection device 140.
• ozone is applied before or at the same time as the waste 10 is heated.
• the method also comprises a step of extraction by the extraction device 150, from a first zone 133 of the tunnel 130, of at least a portion of the atmosphere 133.
• the method can comprise, after the extraction step, at least one reinjection step from a second zone 134 of the tunnel 130 of said portion taken from the atmosphere 133.
• the injection of the ozone takes place in the stirring volume of the waste 10 in the stirring device 160.
• the injection of the ozone takes place before the stirring step of the waste. waste 10 in the brewing device 160.
• the reinjection of the extract portion of atmosphere 133 takes place at an intermediate hopper arranged between the mixing device 160 and the tunnel 130.
• the present invention cleverly employs two disinfection methods, one based on heating the waste and the other on the use of ozone. These two methods are preferably, but not limited to, configured to cooperate together.
• Ozone has a surface disinfectant power and penetrates inside the waste according to its texture.
• Microwaves have a disinfectant power at heart to radiate from the center of each waste to the outside.
• ozone makes it possible to at least partially disinfect the interior of the tunnel.
• ozone has the advantage of oxidizing at least some of the odor molecules generated by the waste, which reduces the nuisance of these odors.
• the present invention allows: a. To disinfect waste by a physicochemical, ozone and heating process, which allows the transformation of infectious risk waste into inert and disinfected waste; b. To disinfect the equipment at the end of the cycle, which increases the safety for users during maintenance; vs. To reduce odor thus allowing easier integration of the equipment.
• the present invention may also include a safety device, in particular in accordance with the regulations for ozone delivered into the air, in order to maintain a predetermined average exposure value, for example over a period of 8 hours, the predetermined average exposure value of ozone to be less than or equal to about 0.1 ppm.
• the commuter system can include a safety device configured to measure, advantageously in real time, the ozone concentration in and / or around the tunnel.
• the safety device is configured to manage the injection device, or even also the extraction device.
• the commuter system in particular the tunnel, is preferably configured to be sealed so as to reduce, or even avoid, any risk of ozone leakage into the atmosphere outside the tunnel.
• the tunnel is preferably configured so as to reduce, or even avoid, any leakage of microwaves.
• the commonality system thus comprises warning sensors arranged around the tunnel, and more generally of all the devices of the system.
• the commuter system comprises at least one air suction device arranged around the tunnel, and advantageously all the equipment of the system which may have an ozone leak. This helps to suck up any ozone leaks.
• the present invention makes it possible to treat a large quantity of waste in a reliable, rapid and efficient manner.

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• Health & Medical Sciences (AREA)
• Animal Behavior & Ethology (AREA)
• Public Health (AREA)
• Veterinary Medicine (AREA)
• Epidemiology (AREA)
• Life Sciences & Earth Sciences (AREA)
• General Health & Medical Sciences (AREA)
• Engineering & Computer Science (AREA)
• Chemical & Material Sciences (AREA)
• General Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Environmental & Geological Engineering (AREA)
• Food Science & Technology (AREA)
• Processing Of Solid Wastes (AREA)
• Apparatus For Disinfection Or Sterilisation (AREA)

Applications Claiming Priority (2)

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• 2020
  • 2020-06-17 FR FR2006320A patent/FR3111572B1/fr active Active
• 2021
  • 2021-06-08 CN CN202180043335.XA patent/CN115768570A/zh active Pending
  • 2021-06-08 WO PCT/EP2021/065272 patent/WO2021254826A1/fr unknown
  • 2021-06-08 US US18/011,009 patent/US20230233720A1/en active Pending
  • 2021-06-08 CA CA3181268A patent/CA3181268A1/fr active Pending
  • 2021-06-08 EP EP21731461.6A patent/EP4168188A1/de active Pending

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