EP2956943B1 - Glassfiber-basket and process for the combustion of waste - Google Patents
Glassfiber-basket and process for the combustion of waste Download PDFInfo
- Publication number
- EP2956943B1 EP2956943B1 EP14704161.0A EP14704161A EP2956943B1 EP 2956943 B1 EP2956943 B1 EP 2956943B1 EP 14704161 A EP14704161 A EP 14704161A EP 2956943 B1 EP2956943 B1 EP 2956943B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- waste
- basket
- envelope
- glass fibre
- metal structure
- 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.)
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Links
- 239000002699 waste material Substances 0.000 title claims description 52
- 238000002485 combustion reaction Methods 0.000 title claims description 30
- 238000000034 method Methods 0.000 title claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 28
- 239000002184 metal Substances 0.000 claims description 27
- 239000007789 gas Substances 0.000 claims description 19
- 239000003365 glass fiber Substances 0.000 claims description 18
- 238000000197 pyrolysis Methods 0.000 claims description 17
- 239000006060 molten glass Substances 0.000 claims description 7
- 238000009941 weaving Methods 0.000 claims description 5
- 239000010815 organic waste Substances 0.000 claims description 4
- 238000004017 vitrification Methods 0.000 claims description 4
- 239000000835 fiber Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 2
- 231100000331 toxic Toxicity 0.000 claims description 2
- 230000002588 toxic effect Effects 0.000 claims description 2
- 230000001186 cumulative effect Effects 0.000 claims 1
- 230000000750 progressive effect Effects 0.000 claims 1
- 239000011152 fibreglass Substances 0.000 description 20
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 229910002091 carbon monoxide Inorganic materials 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 238000009434 installation Methods 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 239000002956 ash Substances 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 2
- 241000287828 Gallus gallus Species 0.000 description 2
- 241001639412 Verres Species 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 231100000701 toxic element Toxicity 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910001868 water Inorganic materials 0.000 description 2
- 206010061218 Inflammation Diseases 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- BKHJHGONWLDYCV-UHFFFAOYSA-N [C]=O.[C] Chemical compound [C]=O.[C] BKHJHGONWLDYCV-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 230000004054 inflammatory process Effects 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 231100001231 less toxic Toxicity 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000010814 metallic waste Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000010811 mineral waste Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- -1 oxides Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000002901 radioactive waste Substances 0.000 description 1
- 238000009958 sewing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/04—Treating liquids
- G21F9/06—Processing
- G21F9/14—Processing by incineration; by calcination, e.g. desiccation
-
- 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
- B09B3/20—Agglomeration, binding or encapsulation of solid waste
-
- 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
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D1/00—Containers having bodies formed in one piece, e.g. by casting metallic material, by moulding plastics, by blowing vitreous material, by throwing ceramic material, by moulding pulped fibrous material, by deep-drawing operations performed on sheet material
- B65D1/38—Baskets or like containers of skeleton or apertured construction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D13/00—Containers having bodies formed by interconnecting two or more rigid, or substantially rigid, components made wholly or mainly of the same material, other than metal, plastics, wood, or substitutes therefor
- B65D13/02—Containers having bodies formed by interconnecting two or more rigid, or substantially rigid, components made wholly or mainly of the same material, other than metal, plastics, wood, or substitutes therefor of glass, pottery, or other ceramic material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/448—Waste feed arrangements in which the waste is fed in containers or the like
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F1/00—Shielding characterised by the composition of the materials
- G21F1/02—Selection of uniform shielding materials
- G21F1/06—Ceramics; Glasses; Refractories
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F5/00—Transportable or portable shielded containers
- G21F5/005—Containers for solid radioactive wastes, e.g. for ultimate disposal
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/28—Treating solids
- G21F9/30—Processing
- G21F9/32—Processing by incineration
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/303—Burning pyrogases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/304—Burning pyrosolids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/40—Stationary bed furnace
Definitions
- the invention relates to the melting and incineration in a furnace of more or less toxic, metallic, organic and inorganic materials and waste such as oxides, glasses, phosphates and metals.
- the metal container containing the waste can be used as a shuttle for introducing the waste into the oven. In this case, it can be cut gradually in the oven, to limit the rate of combustion, but can not be recycled and represents a significant part of the final waste.
- the cutting system for example using a plasma torch, placed in the oven is also complex and expensive.
- An alternative is to place the waste package in a carton that serves as a shuttle. This solution limits the risks in the airlock, but does not solve the problem of the burning speed of the waste package, as soon as the cardboard has burned.
- the object of the invention is therefore to avoid the aforementioned drawbacks relating to the solutions presented above by presenting another method and another device for introducing waste into the furnace.
- a first main object of the invention is a basket for supporting waste to be introduced and incinerated in an incinerator.
- this basket consists, inter alia, of a fiberglass envelope. Ashes from combustion can be melted in the oven, in a bath of molten glass. In this case, the basket consisting in particular of the fiberglass envelope containing the ashes or residues from the waste combustion will be dissolved in the glass bath.
- the first embodiments use a light metal structure to stiffen the basket.
- this metal structure is made by a grid.
- said metal light structure is external and an inner envelope made of glass fibers is placed inside the light metal structure.
- a second embodiment provides that it is the envelope made of glass fibers which is external and the internal light metal structure and therefore placed inside the fiberglass envelope.
- the glass fibers constituting the envelope are woven, the weaving having a mesh size defining a porosity adapted to the type of waste, in order to thermochemically control the pyrolysis rate of this waste.
- the light metal structure is made of wire mesh whose son are integrated in the weaving of the fibers, thus forming a single envelope.
- a second main object of the invention is a vitrification process of waste in a waste vitrification incinerator.
- the fiberglass basket containing the residues of the waste combustion is dissolved in the glass bath.
- the concept according to the invention consists in placing the bag of waste to be incinerated in a basket consisting for the most part of non-woven or woven fiberglass, more or less tightly.
- the tightening of the glass fiber (s) makes it possible to manage the contact between the contained waste and the hot and oxidizing atmosphere inside the incinerator, the weaving allowing for more or less significant heat and gas exchange.
- the basket is preferably stiffened by a light metal structure.
- non-combustible fiberglass with a high melting point enables the mechanical transfer of the waste bag from the airlock introducing waste into the incineration zone, avoiding any loss of contents of the basket during the transfer.
- the contents of the basket namely waste, gradually heat up.
- This rise in temperature leads to the pyrolysis of organic matter.
- the pyrolysis gases escape from the basket to burn in the oxidizing atmosphere of the furnace.
- the choice of the fiberglass envelope constituting, inter alia, the basket, its porosity and weaving more or less tight slows thermal transfers to the inside of the basket and gas transfers to the outside.
- the mesh size of the weave is adapted to the type of waste. This makes it possible to manage the rate of pyrolysis and combustion of the waste contained in the basket. This minimizes the size of the gas puffs generated by the sequential introduction of whole bags of waste into the incinerator.
- the porosity of the fiberglass envelope constituting the basket also makes it possible to minimize ash discharges and non-volatile toxic elements in the gases prevailing inside the incinerator. This porosity can therefore be adapted to the size of the solid toxic particles that must not be entrained in the gases.
- the envelope 10 consisting of fiberglass is placed inside the light metal structure 12.
- the latter is welded to the base of the basket which is advantageously constituted by a 18
- the grill advantageously constituting the light metal structure 12 is preferably cylindrical and is welded, in its upper part on a metal tube 16 for stiffening.
- the dripping pan 18 forming the base of the basket is intended to collect any drops of metal, or other melted materials, if the waste contains this type of low melting point material, which could melt prematurely in the airlock for example (in another type of embodiment the broiler pan could be made of tightly woven glass fibers so as to be virtually liquid-tight).
- the entire basket is completed by a gripping handle 14 fixed in this embodiment on and above the metal tube 16.
- the inner diameter of the fiberglass shell 10 is about 500 mm and is about 750 mm high.
- the weight of the casing is of the order of 1 kg for a fiberglass woven at 45 ° and weight per unit area equal to 600 g / m 2 .
- the broiler pan 18 is preferably made of stainless steel and of a thickness of the order of a millimeter.
- the mesh constituting the light metal structure 12 is a stainless steel wire with a diameter of between 2 and 5 mm.
- the external dimensions important for the handling of the basket in the airlock and in the incineration zone are fixed by the light metal structure 12 used.
- the second embodiment according to the proposed invention uses a fiberglass shell 20 placed outside the metal light structure 22.
- the latter also consists of a cylindrical wire mesh welded at the top to a metal tube 26 which is surmounted by a gripping handle 24.
- the base of the assembly is constituted, preferably by a dripping pan 28 which can be placed inside the casing 20 fiberglass. In this embodiment, filling the basket with waste is facilitated.
- the wires of the mesh constituting the light metallic structure 52 are integrated into the fiberglass weave constituting the envelope 50.
- the broil pan 58 can then be placed inside or outside the envelope 50 made of fiberglass. glass.
- the glass fibers constituting the envelope pass alternately on both sides of the wire mesh constituting the light metal structure 52. This difficult to achieve version brings, however, the advantages of the two previously described embodiments.
- the basket comprises two layers of glass fiber 30A and 30B placed one inside the other.
- the outer layer 30A has the primary function of filtering the pyrolysis gases vis-à-vis the dust.
- the inner layer 30B has the primary function of containing the waste with the appropriate strength properties. It is reported that the function or position of the two layers can also be reversed.
- These two layers 30A and 30B are preferably separated.
- the light metal structure 32 is then placed between these two layers 30A and 30B. Fixing these three elements 30A, 30B and 32 relative to each other can be done by sewing with glass fibers or wire.
- the incineration process according to the invention therefore uses the basket mentioned above to incinerate waste inside an incinerator for a period greater than pyrolysis and combustion of waste without a basket of at least fifteen minutes ( incineration time multiplied by three or ten depending on the basket).
- the waste is thus placed above a bath of molten glass surmounted by a combustion zone under an oxygen atmosphere diluted in argon and heated by an arc plasma transferred between two electrodes.
- the time noted 16:45 the duration of the pyrolysis and combustion is then very short, that is to say say of the order of 3 minutes and the oxygen supply is insufficient to ensure complete combustion of the puff of pyrolysis gas. Indeed, it remains a carbon monoxide content of about 3 to 4% in the reactor outlet gas.
- the waste is kept suspended above a bath of molten glass time noted 15:42. Its burning time is increased to 17 minutes until time noted 15:59. This makes it possible to obtain complete combustion without the presence of carbon monoxide in the outlet gases of the reactor.
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- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- High Energy & Nuclear Physics (AREA)
- Mechanical Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Ceramic Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Thermal Sciences (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Woven Fabrics (AREA)
Description
L'invention concerne la fusion et l'incinération dans un four de matériaux et déchets plus ou moins toxiques, métalliques, organiques et minéraux tels que les oxydes, les verres, les phosphates et les métaux.The invention relates to the melting and incineration in a furnace of more or less toxic, metallic, organic and inorganic materials and waste such as oxides, glasses, phosphates and metals.
Actuellement, plusieurs méthodes sont mises en oeuvre pour incinérer et/ou vitrifier des mélanges de déchets métalliques, organiques et minéraux dans un four à alimentation continue. Les déchets sont broyés en premier lieu, et amenés en continu dans le four. Cette solution présente l'avantage du fonctionnement en continu de l'incinérateur et permet de minimiser le dimensionnement du four et du traitement des gaz. Toutefois, cette solution nécessite un broyage préalable des déchets qui peut être difficile à mettre en oeuvre.Currently, several methods are used to incinerate and / or vitrify metal, organic and mineral waste mixtures in a continuous feed oven. The waste is ground in the first place and fed continuously into the oven. This solution has the advantage of continuous operation of the incinerator and allows to minimize the design of the furnace and the gas treatment. However, this solution requires a preliminary grinding of the waste which can be difficult to implement.
Une deuxième solution consiste à introduire les déchets non broyés par paquets, par l'intermédiaire d'un sas séparant l'atmosphère intérieure du four de l'atmosphère extérieure. Cette deuxième solution évite donc le broyage mais présente de nombreux risques et problèmes, à savoir :
- 1) une manipulation difficile des paquets de déchets dans le sas d'introduction avec un risque de fusion ou d'écoulement des matières organiques dans le sas, suite à la montée en température, lors de l'ouverture de la porte du sas, du côté du four ;
- 2) un risque d'inflammation des matières organiques dans le sas et de surchauffe de ce sas et de ses systèmes de fermeture ;
- 3) un risque de combustion très rapide du paquet de déchets introduit, lors de son introduction dans le four. Ceci nécessite un surdimensionnement de l'alimentation en gaz comburant et de l'installation de traitement des gaz ;
- 4) un risque d'entraînement mécanique de cendres volantes et d'éléments toxiques, lors de la combustion rapide du paquet de déchets.
- 1) a difficult handling of the waste packages in the introduction lock with a risk of merging or flow of organic matter in the airlock, following the rise in temperature, when opening the door of the airlock, the oven side;
- 2) a risk of ignition of organic matter in the airlock and overheating of this airlock and its closure systems;
- 3) a risk of very rapid combustion of the waste package introduced, when introduced into the oven. This requires an oversizing of the combustion gas supply and the gas treatment plant;
- 4) a risk of mechanical entrainment of fly ash and toxic elements during the rapid combustion of the waste package.
Dans l'état actuel de la technique, le conteneur métallique contenant les déchets peut être utilisé comme navette pour l'introduction des déchets dans le four. Dans ce cas, il peut être découpé progressivement dans le four, pour limiter la vitesse de combustion, mais ne peut plus être recyclé et représente une part non négligeable des déchets finaux.In the current state of the art, the metal container containing the waste can be used as a shuttle for introducing the waste into the oven. In this case, it can be cut gradually in the oven, to limit the rate of combustion, but can not be recycled and represents a significant part of the final waste.
Le système de découpe, utilisant par exemple une torche à plasma, placé dans le four est aussi complexe et coûteux. Une alternative consiste à placer le paquet de déchets dans un carton qui sert de navette. Cette solution limite les risques dans le sas, mais ne règle pas le problème de la vitesse de combustion du paquet de déchets, dès que le carton a brûlé.The cutting system, for example using a plasma torch, placed in the oven is also complex and expensive. An alternative is to place the waste package in a carton that serves as a shuttle. This solution limits the risks in the airlock, but does not solve the problem of the burning speed of the waste package, as soon as the cardboard has burned.
Le but de l'invention est donc d'éviter les inconvénients précités relatifs aux solutions présentées ci-dessus en présentant un autre procédé et un autre dispositif d'introduction des déchets dans le four.The object of the invention is therefore to avoid the aforementioned drawbacks relating to the solutions presented above by presenting another method and another device for introducing waste into the furnace.
D'autre part, avec la demande de brevet français
Un premier objet principal de l'invention est un panier destiné à supporter des déchets à introduire et incinérer dans un incinérateur.A first main object of the invention is a basket for supporting waste to be introduced and incinerated in an incinerator.
Selon l'invention, ce panier est constitué, entre autres, d'une enveloppe en fibres de verre. Les cendres provenant de la combustion peuvent être fondues dans le four, au sein d'un bain de verre fondu. Dans ce cas, le panier constitué notamment de l'enveloppe en fibre de verre contenant les cendres ou résidus de la combustion des déchets sera dissout dans le bain de verre.According to the invention, this basket consists, inter alia, of a fiberglass envelope. Ashes from combustion can be melted in the oven, in a bath of molten glass. In this case, the basket consisting in particular of the fiberglass envelope containing the ashes or residues from the waste combustion will be dissolved in the glass bath.
Les premières réalisations utilisent une structure légère métallique pour rigidifier le panier. De préférence, cette structure métallique est réalisée par un grillage.The first embodiments use a light metal structure to stiffen the basket. Preferably, this metal structure is made by a grid.
Selon une première réalisation, ladite structure légère métallique est externe et une enveloppe interne constituée de fibres de verre est placée à l'intérieur de la structure légère métallique.According to a first embodiment, said metal light structure is external and an inner envelope made of glass fibers is placed inside the light metal structure.
Une deuxième réalisation prévoit que ce soit l'enveloppe constituée de fibres de verre qui soit externe et que la structure légère métallique interne et donc placée à l'intérieur de l'enveloppe en fibres de verre.A second embodiment provides that it is the envelope made of glass fibers which is external and the internal light metal structure and therefore placed inside the fiberglass envelope.
Il est prévu également que les fibres de verre constituant l'enveloppe soient tissées, le tissage ayant une taille de maille définissant une porosité adaptée au type de déchets, en vue de contrôler de façon thermochimique la vitesse de pyrolyse de ces déchets.It is also expected that the glass fibers constituting the envelope are woven, the weaving having a mesh size defining a porosity adapted to the type of waste, in order to thermochemically control the pyrolysis rate of this waste.
Dans ce cas, on peut envisager que la structure légère métallique soit constituée de grillage dont les fils sont intégrées au tissage des fibres, formant ainsi une seule et même enveloppe.In this case, it can be envisaged that the light metal structure is made of wire mesh whose son are integrated in the weaving of the fibers, thus forming a single envelope.
Un deuxième objet principal de l'invention est un procédé de vitrification de déchets dans un incinérateur de vitrification de déchets.A second main object of the invention is a vitrification process of waste in a waste vitrification incinerator.
Selon l'invention, il comprend au moins les deux phases consistant à :
- placer les déchets à incinérer dans un panier en fibre de verre tel que défini précédemment pour y être maintenus dans une atmosphère gazeuse, au-dessus d'un bain de verre fondu ; et
- effectuer une pyrolyse et une combustion durant une durée supérieure à une pyrolyse et une combustion de déchets sans panier (la durée d'incinération est multipliée par trois voire dix suivant le panier), permettant ainsi d'obtenir une combustion complète sans présence de monoxyde de carbone dans les gaz de sortie de l'incinérateur.
- placing the waste to be incinerated in a fiberglass basket as defined above to be kept in a gaseous atmosphere, above a bath of molten glass; and
- perform pyrolysis and combustion for a period greater than pyrolysis and combustion of waste without a basket (the incineration time is multiplied by three or even ten depending on the basket), thus allowing to obtain a complete combustion without the presence of carbon monoxide carbon in the exit gases from the incinerator.
De façon préférentielle, après la combustion complète des déchets, le panier en fibre de verre contenant les résidus de la combustion des déchets est dissout dans le bain de verre.Preferably, after complete combustion of the waste, the fiberglass basket containing the residues of the waste combustion is dissolved in the glass bath.
L'invention et ses différentes caractéristiques techniques seront mieux comprises à la lecture de la description qui est accompagnée de plusieurs figures représentant respectivement :
-
figure 1 , en coupe, une première réalisation du panier selon l'invention ; -
figure 2 , en coupe, une deuxième réalisation du panier selon l'invention ; -
figure 3 , en coupe, une troisième réalisation du panier selon l'invention ; -
figure 4 , un graphique explicitant le fonctionnement du procédé selon l'invention ; et -
figure 5 , en coupe, une quatrième réalisation du panier selon l'invention.
-
figure 1 , in section, a first embodiment of the basket according to the invention; -
figure 2 , in section, a second embodiment of the basket according to the invention; -
figure 3 , in section, a third embodiment of the basket according to the invention; -
figure 4 a graph explaining the operation of the method according to the invention; and -
figure 5 , in section, a fourth embodiment of the basket according to the invention.
Le concept selon l'invention consiste à placer le sac de déchets à incinérer dans un panier constitué en grande partie de fibre de verre non tissée ou tissée, de façon plus ou moins serrée. Le serrage de la ou des fibres de verre permet de gérer le contact entre les déchets contenus et l'atmosphère chaude et oxydante à l'intérieur de l'incinérateur, le tissage permettant des échanges thermiques et gazeux plus ou moins importants. Le panier est, de préférence, rigidifié par une structure légère métallique.The concept according to the invention consists in placing the bag of waste to be incinerated in a basket consisting for the most part of non-woven or woven fiberglass, more or less tightly. The tightening of the glass fiber (s) makes it possible to manage the contact between the contained waste and the hot and oxidizing atmosphere inside the incinerator, the weaving allowing for more or less significant heat and gas exchange. The basket is preferably stiffened by a light metal structure.
L'utilisation de la fibre de verre non combustible et ayant un point de fusion élevé permet le transfert mécanique du sac de déchets à partir du sas d'introduction des déchets vers la zone d'incinération, en évitant toute perte de contenu du panier lors du transfert.The use of non-combustible fiberglass with a high melting point enables the mechanical transfer of the waste bag from the airlock introducing waste into the incineration zone, avoiding any loss of contents of the basket during the transfer.
Le principe de l'utilisation de la fibre de verre pour la réalisation du panier est que cette fibre de verre entoure le paquet de déchets et retarde ainsi sa montée en température. Cela évite une fusion et/ou une pyrolyse des déchets organiques trop rapides, notamment pendant le transfert du sas d'introduction vers l'incinérateur.The principle of the use of fiberglass for the realization of the basket is that this glass fiber surrounds the waste package and thus delays its rise in temperature. This avoids a melting and / or pyrolysis of organic waste too fast, especially during the transfer of the airlock to the incinerator.
Dans le four - ou l'incinérateur -, le contenu du panier, à savoir des déchets, chauffe progressivement. Cette montée en température conduit à la pyrolyse des matières organiques. Les gaz de pyrolyse s'échappent du panier pour brûler dans l'atmosphère oxydante du four. Le choix de l'enveloppe en fibre de verre constituant, entre autres, le panier, de sa porosité et de son tissage plus ou moins serré permet de ralentir les transferts thermiques vers l'intérieur du panier et les transferts gazeux vers l'extérieur. Ainsi, on adapte la taille des mailles du tissage au type de déchets. Ceci permet donc de gérer la vitesse de pyrolyse et de combustion des déchets contenus dans le panier. On minimise ainsi la dimension des bouffées de gaz générées par l'introduction séquentielle de sacs entiers de déchets dans l'incinérateur.In the oven - or the incinerator - the contents of the basket, namely waste, gradually heat up. This rise in temperature leads to the pyrolysis of organic matter. The pyrolysis gases escape from the basket to burn in the oxidizing atmosphere of the furnace. The choice of the fiberglass envelope constituting, inter alia, the basket, its porosity and weaving more or less tight slows thermal transfers to the inside of the basket and gas transfers to the outside. Thus, the mesh size of the weave is adapted to the type of waste. This makes it possible to manage the rate of pyrolysis and combustion of the waste contained in the basket. This minimizes the size of the gas puffs generated by the sequential introduction of whole bags of waste into the incinerator.
De plus, la porosité de l'enveloppe en fibre de verre constituant le panier, avec un tissage plus ou moins serré, permet également de minimiser les départs de cendres et des éléments toxiques non volatils dans les gaz régnant à l'intérieur de l'incinérateur. Cette porosité peut donc être adaptée à la dimension des particules toxiques solides qui ne doivent pas être entraînées dans les gaz.In addition, the porosity of the fiberglass envelope constituting the basket, with a more or less tight weave, also makes it possible to minimize ash discharges and non-volatile toxic elements in the gases prevailing inside the incinerator. This porosity can therefore be adapted to the size of the solid toxic particles that must not be entrained in the gases.
En référence à la
Un exemple de cette réalisation prévoit que le diamètre intérieur de l'enveloppe 10 en fibre de verre soit égal à environ 500 mm et qu'il soit d'une hauteur d'environ 750 mm. Dans ce cas, le poids de l'enveloppe est de l'ordre de 1 kg pour une fibre de verre tissée à 45° et de masse surfacique égale à 600 g/m2. La lèchefrite 18 est réalisée, de préférence, en acier inoxydable et d'une épaisseur de l'ordre du millimètre. Le grillage constituant la structure légère métallique 12 est un fil d'acier inoxydable de diamètre compris entre 2 et 5 mm.An example of this embodiment provides that the inner diameter of the
Dans cette première réalisation, les dimensions extérieures importantes pour les manipulations du panier dans le sas et dans la zone d'incinération sont fixées par la structure légère métallique 12 utilisée.In this first embodiment, the external dimensions important for the handling of the basket in the airlock and in the incineration zone are fixed by the
En référence à la
En référence à la
En référence à la
Le procédé d'incinération selon l'invention utilise donc le panier ci-dessus évoqué pour incinérer des déchets à l'intérieur d'un incinérateur pendant une durée supérieure à une pyrolyse et une combustion de déchets sans panier d'au moins quinze minutes (durée d'incinération multipliée par trois voire dix suivant le panier). Les déchets sont ainsi placés au-dessus d'un bain de verre fondu surmonté d'une zone de combustion sous atmosphère d'oxygène dilué dans de l'argon et chauffé par un plasma d'arc transféré entre deux électrodes.The incineration process according to the invention therefore uses the basket mentioned above to incinerate waste inside an incinerator for a period greater than pyrolysis and combustion of waste without a basket of at least fifteen minutes ( incineration time multiplied by three or ten depending on the basket). The waste is thus placed above a bath of molten glass surmounted by a combustion zone under an oxygen atmosphere diluted in argon and heated by an arc plasma transferred between two electrodes.
Sur la
Il faut constater que, dans le cas de l'envoi direct de déchets à la surface d'un bain de verre fondu, au temps noté 16h45, la durée de la pyrolyse et de la combustion est alors très courte, c'est-à-dire de l'ordre de 3 minutes et l'apport d'oxygène est insuffisant pour assurer une combustion complète de la bouffée de gaz de pyrolyse. En effet, il reste une teneur en monoxyde de carbone de l'ordre de 3 à 4% dans les gaz en sortie de réacteur.It should be noted that, in the case of the direct sending of waste to the surface of a bath of molten glass, the time noted 16:45, the duration of the pyrolysis and combustion is then very short, that is to say say of the order of 3 minutes and the oxygen supply is insufficient to ensure complete combustion of the puff of pyrolysis gas. Indeed, it remains a carbon monoxide content of about 3 to 4% in the reactor outlet gas.
Dans le cas de l'utilisation du panier selon l'invention, notamment équipé de son enveloppe en fibre de verre, les déchets sont maintenus suspendus au-dessus d'un bain de verre en fusion au temps noté 15h42. Sa durée de combustion est portée à 17 minutes jusqu'au temps noté 15h59. Ceci permet d'obtenir une combustion complète sans présence de monoxyde de carbone dans les gaz de sortie du réacteur.In the case of the use of the basket according to the invention, in particular equipped with its fiberglass envelope, the waste is kept suspended above a bath of molten glass time noted 15:42. Its burning time is increased to 17 minutes until time noted 15:59. This makes it possible to obtain complete combustion without the presence of carbon monoxide in the outlet gases of the reactor.
Ce résultat est obtenu par l'enveloppe en fibre de verre jouant son rôle de retardateur du début de la combustion 1, ainsi qu'un rôle de ralentisseur de pyrolyse / combustion. Ceci permet d'obtenir une combustion complète des déchets, sans surdimensionner l'installation, notamment l'alimentation en gaz comburant et le traitement des gaz. De plus, on minimise grandement la présence de gaz de combustion à la sortie de l'installation.This result is obtained by the fiberglass envelope acting as a retarder of the start of the combustion 1, and a role of retarder pyrolysis / combustion. This makes it possible to obtain complete combustion of the waste, without oversizing the installation, in particular the supply of oxidizing gas and the treatment of gases. In addition, the presence of flue gas at the outlet of the installation is greatly minimized.
Claims (11)
- Support basket of waste, notably organic, to be inserted into and incinerated in an incinerator, comprising:an envelope (10, 20, 30A, 30B) made of at least a layer of glass fibre stiffened by a lightweight metal structure (12, 22, 32),characterised in that the envelope has a porosity which is defined by the following cumulative criteria, adapted:to maintain the waste in the basket during the introducing of the basket into the incinerator,to thermochemically control the pyrolysis rate of the organic waste, in particular, the progressive temperature rise of the waste until their complete incineration inside the support basket,to filter the pyrolysis gases.
- Basket according to claim 1, characterised in that the layer of glass fibre forming the envelope (10, 20, 30A, 30B) is woven, the weave having a mesh size defining the porosity of the envelope.
- Basket according to any of claim 1 or 2, characterised in that it further comprises a drip pan (18, 28, 58) placed on the ground of the envelope (10).
- Basket according to any of claim 1 to 3, characterised in that the lightweight metal structure (12) is external and that the envelope (10) made of glass fibre is located inside the lightweight metal structure.
- Basket according to any of claim 1 to 3, characterised in that the envelope (20) made of glass fibre is external and in that the lightweight metal structure (22) is located inside the glass fibre envelope.
- Basket according to any of claim 1 to 3, characterised in that the mesh wires forming the lightweight metal structure are integrated into the weaving of the fibre forming at least a layer of the envelope.
- Basket according to any of claim 1 to 6, characterised in that the envelope is composed of two glass fibre layers (30A, 30B), a first outer layer (30A) that will filter pyrolysis gases and a second inner layer (30B) that will contain waste.
- Basket according to claim 7, characterised in that the lightweight metal structure (32) is located between the two glass fibre layers (30A, 30B) of the glass fibre envelope.
- Basket according to any of claim 1 to 4, characterised in that the lightweight metal structure (12, 22, 32) is composed of a mesh.
- Method for incinerating waste, in a waste vitrification incinerator, notably organic waste,
characterised in that it consists of:- placing the waste to be incinerated in a basket according to any one of claims 1 to 9 to be kept in it in a gas atmosphere, above a molten glass bath,- perform a pyrolysis and a combustion, confining toxic particles in the basket for a duration longer than a pyrolysis and combustion of waste without a basket, so that complete combustion can be achieved. - Method according to claim 10, characterised in that after complete combustion of the waste, the glass fibre basket containing waste combustion residues is dissolved in the molten glass bath.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1351262A FR3002075B1 (en) | 2013-02-14 | 2013-02-14 | FIBERGLASS BASKET AND METHOD OF INCINERATING WASTE |
PCT/EP2014/052830 WO2014125030A1 (en) | 2013-02-14 | 2014-02-13 | Fibreglass bin and waste incineration method |
Publications (2)
Publication Number | Publication Date |
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EP2956943A1 EP2956943A1 (en) | 2015-12-23 |
EP2956943B1 true EP2956943B1 (en) | 2018-09-26 |
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Application Number | Title | Priority Date | Filing Date |
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EP14704161.0A Active EP2956943B1 (en) | 2013-02-14 | 2014-02-13 | Glassfiber-basket and process for the combustion of waste |
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US (1) | US9719679B2 (en) |
EP (1) | EP2956943B1 (en) |
JP (1) | JP6279617B2 (en) |
KR (1) | KR102231881B1 (en) |
CN (1) | CN104995689B (en) |
CA (1) | CA2900600C (en) |
ES (1) | ES2703063T3 (en) |
FR (1) | FR3002075B1 (en) |
RU (1) | RU2663875C2 (en) |
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FR3009642B1 (en) | 2013-08-08 | 2018-11-09 | Areva Nc | PROCESS AND INSTALLATION FOR INCINERATION, FUSION AND VITRIFICATION OF ORGANIC AND METAL WASTE |
KR102067465B1 (en) * | 2019-06-24 | 2020-01-17 | 주식회사 티오텍 | Surface tempering apparatus for glass for a foldable dispaly apparatus |
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GB711365A (en) * | 1951-07-06 | 1954-06-30 | Isopad Ltd | Improvements in or relating to electric heating mantles |
US3189510A (en) * | 1959-07-09 | 1965-06-15 | Bendix Corp | Article for forming high tensile strength covering |
DE2457624C3 (en) | 1974-12-06 | 1985-07-18 | Kernforschungszentrum Karlsruhe Gmbh, 7500 Karlsruhe | Plant for sorting and shredding radioactive waste for a packaging press |
GB1589466A (en) * | 1976-07-29 | 1981-05-13 | Atomic Energy Authority Uk | Treatment of substances |
US4240363A (en) * | 1979-08-03 | 1980-12-23 | Troy Stephen R | Incinerator bag |
JPS58109895A (en) * | 1981-12-23 | 1983-06-30 | 株式会社日立製作所 | Solidified material of radioactive waste |
DE3341748A1 (en) * | 1983-11-18 | 1985-05-30 | Kraftwerk Union AG, 4330 Mülheim | METHOD AND OVEN FOR REMOVING RADIOACTIVE WASTE |
JPH0646086B2 (en) * | 1985-04-22 | 1994-06-15 | 有限会社喜立産業 | Sewing oil-free wick |
JPH04253662A (en) * | 1991-01-28 | 1992-09-09 | Matsushita Electric Works Ltd | Packaging container |
JPH07260120A (en) * | 1994-03-25 | 1995-10-13 | Yukio Komatsu | Incinerating method and incinerator |
US6355904B1 (en) * | 1996-06-07 | 2002-03-12 | Science Applications International Corporation | Method and system for high-temperature waste treatment |
DE19714740C1 (en) * | 1997-04-09 | 1998-12-17 | Hampel Christoph | Process and device for the environmentally friendly disposal of toxins, preferably in large containers |
GB9808242D0 (en) * | 1998-04-21 | 1998-06-17 | British Nuclear Fuels Plc | A protective casing |
JP4348796B2 (en) * | 1999-10-27 | 2009-10-21 | 株式会社Ihi | Glass cartridge |
CN201030660Y (en) * | 2007-02-16 | 2008-03-05 | 朱哲正 | Fiber glass reinforced plastic and metallic material compound building material structure |
EP2112423A1 (en) * | 2008-04-25 | 2009-10-28 | Sakowsky, Jon | Multilayer container for liquids and gases storing under the elevated pressure and method of production thereof |
FR2934183B1 (en) | 2008-07-28 | 2011-02-11 | Commissariat Energie Atomique | PROCESS FOR CONTAINING WASTE BY VITRIFICATION IN METAL POTS. |
DE102011085480A1 (en) * | 2011-10-28 | 2013-05-02 | Volkmar Gräf | CONTAINER SYSTEM FOR THE END STORAGE OF RADIOACTIVE WASTE AND / OR POISONOIL |
FR3009642B1 (en) * | 2013-08-08 | 2018-11-09 | Areva Nc | PROCESS AND INSTALLATION FOR INCINERATION, FUSION AND VITRIFICATION OF ORGANIC AND METAL WASTE |
-
2013
- 2013-02-14 FR FR1351262A patent/FR3002075B1/en not_active Expired - Fee Related
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2014
- 2014-02-13 KR KR1020157024730A patent/KR102231881B1/en active IP Right Grant
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- 2014-02-13 JP JP2015557428A patent/JP6279617B2/en active Active
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- 2014-02-13 EP EP14704161.0A patent/EP2956943B1/en active Active
- 2014-02-13 ES ES14704161T patent/ES2703063T3/en active Active
- 2014-02-13 CA CA2900600A patent/CA2900600C/en active Active
- 2014-02-13 RU RU2015138153A patent/RU2663875C2/en active
- 2014-02-13 WO PCT/EP2014/052830 patent/WO2014125030A1/en active Application Filing
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CA2900600A1 (en) | 2014-08-21 |
CN104995689A (en) | 2015-10-21 |
RU2663875C2 (en) | 2018-08-13 |
FR3002075A1 (en) | 2014-08-15 |
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WO2014125030A1 (en) | 2014-08-21 |
EP2956943A1 (en) | 2015-12-23 |
US20150369480A1 (en) | 2015-12-24 |
JP6279617B2 (en) | 2018-02-14 |
CA2900600C (en) | 2023-02-14 |
KR102231881B1 (en) | 2021-03-25 |
FR3002075B1 (en) | 2015-03-06 |
JP2016515915A (en) | 2016-06-02 |
CN104995689B (en) | 2018-01-30 |
RU2015138153A (en) | 2017-03-13 |
ES2703063T3 (en) | 2019-03-06 |
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