EP0593665B1 - Incineration method, particularly for spent graphite - Google Patents
Incineration method, particularly for spent graphite Download PDFInfo
- Publication number
- EP0593665B1 EP0593665B1 EP92915960A EP92915960A EP0593665B1 EP 0593665 B1 EP0593665 B1 EP 0593665B1 EP 92915960 A EP92915960 A EP 92915960A EP 92915960 A EP92915960 A EP 92915960A EP 0593665 B1 EP0593665 B1 EP 0593665B1
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- Prior art keywords
- suspension
- combustion
- graphite
- incineration
- solid
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- 238000000034 method Methods 0.000 title claims abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title description 15
- 229910002804 graphite Inorganic materials 0.000 title description 14
- 239000010439 graphite Substances 0.000 title description 14
- 238000002485 combustion reaction Methods 0.000 claims abstract description 19
- 239000000725 suspension Substances 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims abstract description 11
- 239000002245 particle Substances 0.000 claims abstract description 11
- 239000007800 oxidant agent Substances 0.000 claims abstract description 4
- 230000001590 oxidative effect Effects 0.000 claims abstract description 4
- 239000000654 additive Substances 0.000 claims abstract description 3
- 239000012736 aqueous medium Substances 0.000 claims abstract description 3
- 239000007788 liquid Substances 0.000 claims abstract description 3
- 239000007787 solid Substances 0.000 claims description 12
- 239000001301 oxygen Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000007789 gas Substances 0.000 claims description 7
- 238000005187 foaming Methods 0.000 claims description 3
- 239000004094 surface-active agent Substances 0.000 abstract description 3
- 239000011236 particulate material Substances 0.000 abstract 1
- 239000011343 solid material Substances 0.000 abstract 1
- 239000003517 fume Substances 0.000 description 11
- 239000006260 foam Substances 0.000 description 10
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 9
- 239000000047 product Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 229910001868 water Inorganic materials 0.000 description 7
- 239000002699 waste material Substances 0.000 description 5
- 238000000227 grinding Methods 0.000 description 3
- 238000010348 incorporation Methods 0.000 description 3
- 239000007900 aqueous suspension Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 239000006265 aqueous foam Substances 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 230000008033 biological extinction Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007792 gaseous phase Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Images
Classifications
-
- 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
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/18—Radioactive materials
Definitions
- the present invention relates to a process for preparing for its incineration graphite, in particular irradiated graphite and more generally a combustible material, such as waste, with a limited production of fumes, in order to avoid a significant and costly treatment of these.
- the invention proposes a process for the preparation prior to an incineration of a combustible material.
- the oxidizing gas can be oxygen or enriched air and the pressure of the foam obtained will be of the order of 2 to 10 bars, depending on either the opening of a control valve located before the combustion furnace, i.e. the pressure in the furnace and the pressure drop between the pump outlet and the combustion furnace.
- the maximum of the solid fraction (from 35 to 45% by weight of the suspension) will depend on the apparent density of the pulverized solid and on its lower calorific value. For example, since graphite has a high calorific value and an apparent density, the solid fraction will be of the order of 35%. For lower criteria, the fraction may be higher without damaging the pumpable nature of the product or leading to too hot combustion.
- the material to be incinerated contains radioactive particles, and that a fraction of these particles will be entrained by the combustion fumes, it is completely essential to treat these fumes with the outlet from the incinerator, and the treatment process will be all the more economical as the volume of smoke will be as small as possible.
- the diagram shown in the drawing illustrates a processing and incineration chain for a crude product 1, which in this case is graphite.
- the first step in processing this product consists of grinding 2. Grinding can consist of several stages using several types of apparatus so as to obtain an output powdery product with an appropriate particle size (for example 80% of the particles whose diameter is less than 200 ⁇ ). This grinding can be carried out in a humid environment to avoid the release of dust and reduce the risk of explosion which results therefrom, and also to obtain a fluid which is transportable by means of pumps.
- the powdered graphite obtained at the outlet of the mills 2 is added with water in a mixer 3.
- a pump 4 With the aid of a pump 4, the continuous circulation of the product coming from the mixer 3 is ensured in the direction for example of a concentration 5 (acting by measuring viscosity for example) to arrive at a mixer 6 for adjusting this concentration by adding water.
- the product leaving this mixer 6 will have a content at most equal to 35% of solid particles.
- This is a relatively charged aqueous suspension which is very easily pumpable.
- This suspension is using a pump 7 introduced into a mixer 8 intended to produce a three-phase liquid-solid-gas mixture. To do this, is introduced into the mixer, in addition to the suspension to be transformed into foam, surfactant additives 9 and a swelling gas 10. In the present case the gas will be oxygen.
- a pressure control valve 11 downstream of the pump or to the pressure drop in the circuit it is possible to obtain a pressurized foam, for example between 2 and 10 bars.
- the pressurization of the foam has a double advantage: firstly it becomes self-propelling by partial expansion in the supply lines 12 of a combustion hearth 13, and secondly the relaxation of this foam in the hearth promotes his injection.
- the hearth 13 is a cyclone hearth known in itself which has the advantages mentioned above with regard to the residence time of the particles and the relative gas-solid speed, in order to achieve complete combustion of the product.
- Oxygen 14 is introduced into the hearth 13 as combustion gas. It should be noted that the combustion may include a post-combustion stage. The ashes are collected in an ashtray 15 while the fumes 16 are led into a water cooler 17 which makes it possible to condense the water vapor produced by combustion. This cooler will include a demister that retains water droplets.
- the fumes thus freed from the aqueous effluents pass through a heater 18 which places them at a temperature above the dew point to avoid any condensation which could be harmful to the operation of the very high efficiency filters 19 through which the fumes pass.
- filters 19 make it possible to trap the solid residues 20 while the gaseous phase of the fumes is transmitted to the atmosphere by an extraction fan and a chimney 22.
- This table shows a 60% reduction in the mass flow rate of the fumes produced by the combustion of graphite in a cyclone hearth compared to those in a fluidized bed.
- the fumes leaving the cyclone hearth contain almost 50% water.
- the fumes to be treated before discharge into the atmosphere are 78% less in mass during an incineration in a cyclone hearth than during an incineration in a fluidized bed. It is therefore understandable that the filtration and purification installations are much less important in one technique than in the other.
- aqueous foam greatly facilitates the control of the incineration hearth since the production of water vapors tends to lower the temperature and the regulation of the solid load of the foam makes it possible to achieve simple regulation of the operation of the oven, or even its extinction in an emergency if the solid fuel is completely removed from the foam.
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- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- High Energy & Nuclear Physics (AREA)
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
- Carbon And Carbon Compounds (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Air Supply (AREA)
Abstract
Description
La présente invention concerne un procédé pour préparer en vue de son incinération du graphite, notamment du graphite irradié et plus généralement un matériau combustible, tel qu'un déchet, avec une production de fumées limitée, afin d'éviter un traitement important et coûteux de cellesci.The present invention relates to a process for preparing for its incineration graphite, in particular irradiated graphite and more generally a combustible material, such as waste, with a limited production of fumes, in order to avoid a significant and costly treatment of these.
L'incinération des déchets est l'une des méthodes les plus employées pour les dégrader. La protection de l'environnement impose cependant des contraintes de plus en plus sévères en ce qui concerne les rejets dans l'atmosphère, ce qui conduit à des installations de traitement des fumées importantes pour retenir les éléments indésirables et/ou polluants.One of the most widely used methods of degrading waste is incineration. Environmental protection however imposes increasingly severe constraints with regard to discharges into the atmosphere, which leads to large smoke treatment installations for retaining undesirable and / or polluting elements.
Il est donc utile de produire un minimum de fumées de manière à diminuer les volumes à traiter en sortie d'incinérateur.It is therefore useful to produce a minimum of fumes so as to reduce the volumes to be treated at the outlet of the incinerator.
Il est également utile d'éviter la production de composants gazeux nocifs (par exemple des oxydes d'azote) au cours de l'incinération et l'un des moyens permettant de limiter cette production est de limiter la température de combustion.It is also useful to avoid the production of harmful gaseous components (for example nitrogen oxides) during incineration and one of the ways to limit this production is to limit the combustion temperature.
Il est enfin avantageux de pouvoir procéder à une combustion complète et de disposer d'une cinétique de réaction rapide.Finally, it is advantageous to be able to carry out complete combustion and to have rapid reaction kinetics.
On citera à cet effet le document US-A-38 48 548 qui décrit un procédé de préparation de déchets solides explosifs à incinérer consistant à diviser les déchets puis à former une suspension aqueuse de ces déchets qui est introduite dans un incinérateur rotatif selon une combustion particulière avec apport de comburant. L'essentiel des résultats obtenus par ce procédé vient à l'incinérateur rotatif dont le bon fonctionnement eest le gage d'une pollution minimale. Les effets de l'invention sont en revanche indépendants des conditions de marche d'un matériel.For this purpose, document US-A-38 48 548 which describes a process for preparing explosive solid waste to be incinerated, consisting of dividing the waste and then forming an aqueous suspension of this waste which is introduced into a rotary incinerator according to combustion. particular with addition of oxidizer. Most of the results obtained by this process come from the rotary incinerator, the proper functioning of which guarantees minimal pollution. The effects of the invention are, however, independent of the operating conditions of equipment.
Dans le but d'atteindre ces objectifs, l'invention propose un procédé de préparation préalable à une incinération d'un matériau combistible.In order to achieve these objectives, the invention proposes a process for the preparation prior to an incineration of a combustible material.
Ainsi, conformément à l'invention, le procédé comporte, avant la combustion, la réalisation en continu des étapes suivantes :
- division du matériau en particules,
- incorporation du matériau divisé dans un milieu aqueux additionné de produits moussants (tensio-actifs) à raison d'un maximum de 35 % à 45% en poids de solide selon la nature du solide considéré,
- élévation en pression de la suspension ainsi obtenue,
- et moussage de la suspension sous pression réalisé par incorporation d'un gaz comburant sous pression.
- division of the material into particles,
- incorporation of the divided material in an aqueous medium supplemented with foaming products (surfactants) at a rate of a maximum of 35% to 45% by weight of solid depending on the nature of the solid considered,
- pressure rise of the suspension thus obtained,
- and foaming the suspension under pressure by incorporating an oxidizing gas under pressure.
Le gaz comburant peut être de l'oxygène ou de l'air enrichi et la pression de la mousse obtenue sera de l'ordre de 2 à 10 bars, en fonction, soit de l'ouverture d'une vanne de régulation située avant le foyer de combustion, soit de la pression dans le foyer et de la perte de charge entre la sortie de la pompe et le foyer de combustion.The oxidizing gas can be oxygen or enriched air and the pressure of the foam obtained will be of the order of 2 to 10 bars, depending on either the opening of a control valve located before the combustion furnace, i.e. the pressure in the furnace and the pressure drop between the pump outlet and the combustion furnace.
Le maximum de la fraction solide ( de 35 à45% en poids de la suspension) dépendra de la masse volumique apparente du solide pulvérisé et de son pouvoir calorifique inférieur. Par exemple, le graphite ayant un pouvoir calorifique et une masse volumique apparente élevés, la fraction solide sera de l'ordre de 35%. Pour des critères plus faibles, la fraction pourra être plus élévée sans que celà nuise au caractère pompable du produit ni conduise à une combustion trop chaude.The maximum of the solid fraction (from 35 to 45% by weight of the suspension) will depend on the apparent density of the pulverized solid and on its lower calorific value. For example, since graphite has a high calorific value and an apparent density, the solid fraction will be of the order of 35%. For lower criteria, the fraction may be higher without damaging the pumpable nature of the product or leading to too hot combustion.
D'autres caractéristiques et avantages de l'invention ressortiront de la description d'un mode de réalisation donné ci-après à titre d'exemple, appliqué à l'incinération du graphite et notamment du graphite irradié.Other characteristics and advantages of the invention will emerge from the description of an embodiment given below by way of example, applied to the incineration of graphite and in particular irradiated graphite.
Il sera fait référence au dessin annexé qui représente par une figure unique le schéma du procédé mis en oeuvre par l'invention.Reference will be made to the appended drawing which represents by a single figure the diagram of the process implemented. work by the invention.
Il existe actuellement un besoin de traiter par incinération le graphite usagé et irradié provenant du démantèlement de réacteurs nucléaires. Ce graphite se présente sous deux formes géométriques, en briques et en tubes. La qualité nucléaire du matériau est telle qu'il ne contient pratiquement que du carbone pur ; les impuretés sont en concentration très faibles. Afin de réduire le volume de ce graphite à stocker sous forme de déchets, il a été proposé de le broyer et de l'incinérer. Il a été en effet montré que la combustion est d'autant plus complète que le diamètre des particules est faible, que le temps de séjour dans le foyer de ces particules est important et que la vitesse relative gaz-solide est également importante.There is currently a need to incinerate used and irradiated graphite from the dismantling of nuclear reactors. This graphite comes in two geometric forms, in bricks and in tubes. The nuclear quality of the material is such that it contains practically only pure carbon; the impurities are in very low concentration. In order to reduce the volume of this graphite to be stored as waste, it has been proposed to crush and incinerate it. It has indeed been shown that the combustion is all the more complete the smaller the diameter of the particles, the longer the residence time in the focus of these particles and the greater the gas-solid speed is also important.
Pour satisfaire à ces conditions, il a été retenu un foyer de type cyclone bien que ce foyer ne soit pas une solution parfaite à tous les problèmes rencontrés lors de cette combustion, notamment par le transport du solide divisé en particules très fines, et d'autre part du fait de la génération d'oxydes d'azote toxiques.To meet these conditions, a cyclone type firebox has been chosen, although this firebox is not a perfect solution to all the problems encountered during this combustion, in particular by the transport of the solid divided into very fine particles, and of on the other hand due to the generation of toxic nitrogen oxides.
Par ailleurs, compte tenu du fait que le matériau à incinérer comporte des particules radio-actives, et qu'une fraction de ces particules se retrouveront entraînées par les fumées de la combustion, il est tout-à-fait indispensable de traiter ces fumées à la sortie de l'incinérateur, et le procédé de traitement sera d'autant plus économique que le volume de fumées sera le plus réduit possible.Furthermore, given the fact that the material to be incinerated contains radioactive particles, and that a fraction of these particles will be entrained by the combustion fumes, it is completely essential to treat these fumes with the outlet from the incinerator, and the treatment process will be all the more economical as the volume of smoke will be as small as possible.
La réponse à ces contraintes réside, selon l'invention, dans la préparation du combustible.The answer to these constraints, according to the invention, lies in the preparation of the fuel.
Le schéma représenté au dessin illustre une chaîne de traitement et d'incinération d'un produit brut 1, qui dans le cas d'espèce, est du graphite. La première étape du traitement de ce produit consiste en un broyage 2. Le broyage peut consister en plusieurs étapes mettant en oeuvre plusieurs types d'appareils de manière à obtenir en sortie un produit pulvérulent de granulométrie appropriée (par exemple 80 % des particules dont le diamètre est inférieur à 200 µ). Ce broyage peut être réalisé en milieu humide pour éviter les dégagements de poussières et diminuer les risques d'explosion qui en résultent, et également obtenir une fluide qui est transportable au moyen de pompes.The diagram shown in the drawing illustrates a processing and incineration chain for a
Le graphite pulvérulent obtenu à la sortie des broyeurs 2 est additionné d'eau dans un mélangeur 3. A l'aide d'une pompe 4, la circulation continue du produit issu du mélangeur 3 est assurée en direction par exemple d'un détecteur de concentration 5 (agissant par mesure de la viscosité par exemple) pour aboutir à un mélangeur 6 d'ajustement de cette concentration par addition d'eau. Le produit sortant de ce mélangeur 6 aura une teneur au plus égale à 35 % de particules solides. Il s'agit là d'une suspension aqueuse relativement chargée qui est très facilement pompable. Cette suspension est à l'aide d'une pompe 7 introduite dans un mélangeur 8 destiné à fabriquer un mélange triphasique liquide-solide-gaz. Pour ce faire, on introduit dans le mélangeur, outre la suspension à transformer en mousse, des adjuvents tensio-actifs 9 et un gaz de foisonnement 10. Dans le cas présent le gaz sera de l'oxygène.The powdered graphite obtained at the outlet of the
Grâce à une vanne de régulation de pression 11 en aval de la pompe ou à la perte de charge du circuit, on peut obtenir une mousse pressurisée, par exemple entre 2 et 10 bars. La pressurisation de la mousse présente un double intérêt : tout d'abord elle devient autopropulsive par détente partielle dans les conduites d'alimentation 12 d'un foyer de combustion 13, et d'autre part la détente de cette mousse dans le foyer en favorise son injection.Thanks to a
Le foyer 13 est un foyer cyclone connu en lui-même qui présente les avantages rappelés ci-dessus en ce qui concerne le temps de séjour des particules et la vitesse relative gaz-solide, pour accéder à une combustion complète du produit. De l'oxygène 14 est introduit dans le foyer 13 comme gaz de combustion. On notera que la combustion peut comporter un étage de post-combustion. Les cendres sont recueillies dans un cendrier 15 tandis que les fumées 16 sont conduites dans un refroidisseur à eau 17 qui permet de condenser la vapeur d'eau produite par la combustion. Ce refroidisseur incluera un dévésiculiseur retenant les gouttelettes d'eau. Les fumées ainsi débarrassées des effluents aqueux, passent dans un réchauffeur 18 qui les place à une température au-dessus du point de rosée pour éviter toute condensation qui pourrait être nuisible au fonctionnement des filtres à très haute efficacité 19 traversés par les fumées. Ces filtres permettent de piéger les résidus solides 20 tandis que la phase gazeuse des fumées est transmise à l'atmosphère par un ventilateur d'extraction et une cheminée 22.The
Afin d'illustrer l'intérêt de la préparation du graphite sous forme d'une mousse chargée à base aqueuse (mélange triphasique eau, oxygène, graphite), on donnera ci-après des éléments comparatifs entre une incinération réalisée au moyen d'une technologie connue (par exemple en lit fluidisé) et une incinération par foyer cyclone avec le combustible introduit sous forme de mousse.
On remarque de ce tableau une réduction de 60 % du débit massique des fumées produites par la combustion du graphite en foyer cyclone par rapport à celles en lit fluidisé. En outre, les fumées en sortie du foyer cyclone contiennent pratiquement 50 % d'eau. Ainsi les fumées à traiter avant rejet dans l'atmosphère sont 78 % moins importantes en masse lors d'une incinération dans un foyer cyclone que lors d'une incinération en lit fluidisé. On comprend donc que les installations de filtration et d'épuration sont beaucoup moins importantes dans une technique que dans l'autre.This table shows a 60% reduction in the mass flow rate of the fumes produced by the combustion of graphite in a cyclone hearth compared to those in a fluidized bed. In addition, the fumes leaving the cyclone hearth contain almost 50% water. Thus, the fumes to be treated before discharge into the atmosphere are 78% less in mass during an incineration in a cyclone hearth than during an incineration in a fluidized bed. It is therefore understandable that the filtration and purification installations are much less important in one technique than in the other.
De ce tableau on comprend également l'intérêt de procéder, d'une part à la formation d'une mousse à partir d'oxygène (bien que cet oxygène ne représente que moins de 4% de l'oxygène nécessaire à la combustion du produit) et d'autre part et surtout, à utiliser comme comburant de l'oxygène pur : on évite ainsi la production d'oxydes d'azote.From this table we also understand the advantage of proceeding, on the one hand, to the formation of a foam from oxygen (although this oxygen represents only less than 4% of the oxygen necessary for the combustion of the product ) and secondly and above all, to be used as an oxidizer for pure oxygen: this avoids the production of nitrogen oxides.
L'utilisation d'une mousse aqueuse facilite grandement la conduite du foyer d'incinération puisque la production de vapeurs d'eau tend à abaisser la température et la régulation de la charge en solide de la mousse permet de réaliser une régulation simple du fonctionnement du four, voire son extinction en cas d'urgence si on supprime totalement le solide combustible de la mousse.The use of an aqueous foam greatly facilitates the control of the incineration hearth since the production of water vapors tends to lower the temperature and the regulation of the solid load of the foam makes it possible to achieve simple regulation of the operation of the oven, or even its extinction in an emergency if the solid fuel is completely removed from the foam.
Enfin, on ajoutera qu'il est possible d'inclure une fraction relativement faible de liquide combustible pollué (par exemple une huile usagée ou contaminée) dans la suspension avant foisonnement.Finally, it will be added that it is possible to include a relatively small fraction of polluted combustible liquid (for example a used or contaminated oil) in the suspension before expansion.
Claims (2)
- A method of preparing a combustible material (1) with a view to its incineration, characterized in that it comprises before combustion (13) the continuous performance of the following steps:. dividing (2) the material into particles,. incorporating (3) the divided material into an aqueous medium at a maximum rate of 35% to 45% by weight of solid relative to the liquid,. increasing the pressure of the suspension thereby obtained, and. foaming the suspension under pressure, by incorporating an oxidizing gas (10) and surface-active additives (9) in a mixer (8) of the suspension.
- A method according to claim 1, characterized in that the oxidizer gas is oxygen.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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FR9108899A FR2679320B1 (en) | 1991-07-15 | 1991-07-15 | PROCESS FOR THE INCINERATION OF MATERIALS, ESPECIALLY IRRADIATED GRAPHITE. |
FR9108899 | 1991-07-15 | ||
PCT/FR1992/000659 WO1993002321A1 (en) | 1991-07-15 | 1992-07-09 | Incineration method, particularly for spent graphite |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0593665A1 EP0593665A1 (en) | 1994-04-27 |
EP0593665B1 true EP0593665B1 (en) | 1996-02-21 |
Family
ID=9415106
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP92915960A Expired - Lifetime EP0593665B1 (en) | 1991-07-15 | 1992-07-09 | Incineration method, particularly for spent graphite |
Country Status (8)
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EP (1) | EP0593665B1 (en) |
JP (1) | JPH0697088B2 (en) |
AT (1) | ATE134432T1 (en) |
CA (1) | CA2113109C (en) |
DE (1) | DE69208467T2 (en) |
ES (1) | ES2085632T3 (en) |
FR (1) | FR2679320B1 (en) |
WO (1) | WO1993002321A1 (en) |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3516777A (en) * | 1968-07-26 | 1970-06-23 | Prenco Mfg Co | Apparatus for supplying mixture of burnable fluid waste material and air to incinerator burner |
US3848548A (en) * | 1973-11-27 | 1974-11-19 | Hercules Inc | Incineration process for disposal of waste propellant and explosives |
FR2318385A1 (en) * | 1975-07-16 | 1977-02-11 | Creusot Loire | PROCESS AND INSTALLATION FOR RECOVERING COMBUSTIBLE LIQUID WASTE |
-
1991
- 1991-07-15 FR FR9108899A patent/FR2679320B1/en not_active Expired - Fee Related
-
1992
- 1992-07-09 DE DE69208467T patent/DE69208467T2/en not_active Expired - Fee Related
- 1992-07-09 CA CA002113109A patent/CA2113109C/en not_active Expired - Fee Related
- 1992-07-09 EP EP92915960A patent/EP0593665B1/en not_active Expired - Lifetime
- 1992-07-09 JP JP5502617A patent/JPH0697088B2/en not_active Expired - Lifetime
- 1992-07-09 WO PCT/FR1992/000659 patent/WO1993002321A1/en active IP Right Grant
- 1992-07-09 ES ES92915960T patent/ES2085632T3/en not_active Expired - Lifetime
- 1992-07-09 AT AT92915960T patent/ATE134432T1/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
JPH0697088B2 (en) | 1994-11-30 |
CA2113109A1 (en) | 1993-02-04 |
FR2679320B1 (en) | 1993-10-15 |
ES2085632T3 (en) | 1996-06-01 |
DE69208467T2 (en) | 1996-09-05 |
CA2113109C (en) | 1997-01-21 |
DE69208467D1 (en) | 1996-03-28 |
ATE134432T1 (en) | 1996-03-15 |
EP0593665A1 (en) | 1994-04-27 |
FR2679320A1 (en) | 1993-01-22 |
WO1993002321A1 (en) | 1993-02-04 |
JPH06503874A (en) | 1994-04-28 |
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