Classifications

• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
  • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
  • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
  • C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
  • C10B7/00—Coke ovens with mechanical conveying means for the raw material inside the oven
  • C10B7/14—Coke ovens with mechanical conveying means for the raw material inside the oven with trucks, containers, or trays
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
  • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S423/00—Chemistry of inorganic compounds
  • Y10S423/18—Treating trash or garbage

Definitions

• Waste treatment plant by injecting hot gases into the load to be treated and recycling of the thermolysis gases produced
• the present invention relates, in general, to the treatment by thermolysis of solid products or waste the discharge of which is harmful to the environment.
• an installation for the treatment of solid products whose discharge is detrimental to the environment comprising, in general, a dehydration zone into which the solid products, a thermolysis zone downstream from the dehydration zone, an exit and cooling zone for solid residues and pumping means communicating by an extraction line with the thermolysis zone to maintain it in vacuum and to vacuum it thermolysis gases.
• thermolytic transformation In order to be able to carry out the thermolytic transformation in the total absence of free oxygen, the dehydration, thermolysis and cooling zones were formed by chambers insulated from one another in a substantially sealed manner.
• the dehydration and thermolysis chambers were provided with heating means, such as catalytic radiant panels or flame burners using thermolysis gases and / or commercial combustible gases (inexpensive).
• heating means such as catalytic radiant panels or flame burners using thermolysis gases and / or commercial combustible gases (inexpensive).
• the heating of the chambers of these chambers was thus ensured, in the case of burners, by the radiation of the interior wall of the chambers heated by the flames of the burners. Heating was then also ensured by convection of gas in the environment of the load of products to be treated, convection ensured by expansion of the gases generated in the corresponding chamber.
• the catalytic radiant panels were supplied, on the one hand, with pure oxygen or with air and, on the other hand, with thermolysis gas originating from thermolytic decomposition.
• thermolysis gas originating from thermolytic decomposition.
• the carbon dioxide and water vapor generated by the oxidation of the thermolysis gases in the catalytic radiant panels could participate in the heating by convection and radiation.
• thermolysis chamber was kept for example around 600 ° C while that of the dehydration chamber, lower, was kept above 100 ° C, for example around 120 ° C.
• the solid products to be treated were brought by carriages, moved within the chambers by a mechanical system of the pinion and rack type, for example, or even of the type with electromagnetic drive. These carts were also designed so that solid residues - glass, rubble, metals, for example - remain in the carts while being easily removed at the outlet of the cooling chamber.
• thermolysis process turns out to be far from perfect, in that there are in particular a certain number of unburnt residues after the thermolysis step.
• thermolysis step It aims, in general, to improve the thermolysis step.
• It also relates to an installation for the treatment of solid products, the discharge of which is harmful to the environment, which is self-sufficient from an energy point of view.
• the present invention aims to provide an installation which is the least polluting possible, which makes it possible to recover easily storable products and requires a minimum of maintenance.
• an installation for the treatment of solid products comprising a chamber for thermolysis of solid products by the addition of heat, a hot gaseous fluid supply line constituting the heat supply, opening into the chamber, a gas extraction line from the thermolysis zone, a carriage for bringing the solid products within this chamber, connection means fluids adapted to establish a temporary fluid connection between the supply line and a connection zone provided on the carriage and communicating with the zone for receiving the solid products from the carriage, characterized in that it comprises a boiler fluidly connected to the line extraction and adapted to burn at least part of the gases from the thermolysis chamber and a means for recycling the combustion gases from the boiler to produce the hot gaseous fluid.
• the invention thus teaches to replace the burners or catalytic radiant panels by introducing a hot gaseous fluid directly into the charge of waste to be treated. This avoids any creation of hot spots or a possible explosive reaction between oxygen and hydrogen. In addition, bringing the gas directly to the load reduces the risk of unburnt.
• thermolysis gases formed in the thermolysis chamber are used in the production of hot gaseous fluid intended to be introduced into this same chamber.
• the hot gaseous fluid may advantageously include combustion gases from the boiler, thermolysis gases formed in the chamber and extracted beforehand therefrom by the extraction line, gases resulting from the treatment of thermolysis gases formed in the chamber and extracted beforehand by the extraction line or an inert gas (nitrogen, etc.).
• the installation further comprises a heat exchanger disposed downstream of the extraction line, in which the gases extracted from the thermolysis zone are passed through the extraction line, as hot fluid, a fractionation train disposed downstream of the heat exchanger, in which the gases cooled by the heat exchanger to obtain separate fractions containing, respectively, heavy hydrocarbons, light hydrocarbons, water and uncondensed gases at low temperature, a recycling line connected to the heat exchanger, downstream of the fractionation train , so as to bring a part of the uncondensed gases at low temperature into the heat exchanger, as cold fluid, to raise the temperature, this recycling line being connected to the supply line and passing through the boiler for reheat the gases circulating in this recycling line by combustion of another part of the uncondensed gases at low temperature in the boiler.
• the carriage comprises a tank with nozzles opening out, in a regularly distributed manner, from the bottom of the tank and fluidly connected by a tubular system to the connection area
• the fluidic connection means comprise a mobile telescopic device between a position for fluid connection to the connection area of a pipe surmounted by a bellows and the other end of which is connected to the supply line and a position away from the carriage
• the bellows is mounted on the telescopic device with the possibility of angular movement of the end of the bellows intended to be applied to the connection area
• the installation also includes pumping means communicating by an extraction line with the chamber
• the carriage is provided with displacement rails on which the tubular system is mounted and defined rollers ant a raceway for the carriage are mounted in the chamber.
• the trolley comprises a tank with a grid forming the area for receiving solid products
• the trolley comprises a tank provided with a gas-permeable bottom forming the area for receiving solid products and the fluid connection means form, with this bottom, a double bottom, in the connection position.
• FIG. 1 is a schematic view of an installation according to a mode of preferred embodiment of the present invention
• Figure 2 is a schematic elevational view with cross section of the dehydration and thermolysis chamber of the installation for the treatment of solid products of Figure 1
• - Figure 3 is a schematic elevational view with longitudinal section of the chamber of Figure 2
• FIG. 4 is a plan view from above of part of a carriage forming part of the chamber illustrated in FIGS. 2 and 3.
• FIG. 1 The installation of FIG. 1 comprises an airlock 100 into which the solid products penetrate, then a thermolysis chamber 200 in which the solid products are first partially or completely dehydrated, then brought to their thermal decomposition temperature (known and fixed at advance) for example around 400 ° C (typically between 250 ° C and 750 ° C).
• the thermolytic transformation is advantageously carried out in the total absence of free oxygen.
• this thermolysis chamber is followed by a cooling zone 300 where the solid residues from the heat treatment are brought to room temperature, for example by spraying water. Furthermore, an emptying zone 400 of the carriages 2 is provided, after the cooling zone 300. The residues are poured into a swimming pool 500 from which they are then extracted, then sorted.
• the zones 100, 200 and 300 are chambers insulated from one another in a substantially sealed manner, for example by guillotine doors 101 actuated by jacks; the doors between chambers 100 and 200, 200 and 300 and 300 and 400 being movable transversely in sealed housings (registers).
• watertight doors are provided at the entrance to the chamber 100 and at the exit from the chamber 400, whereby the airlock 100 and the drainage area 400 are, at will, isolated from the outside. ; they can be movable vertically or horizontally or around a joint according to the dimensions of the installation, the space available and the free choice of the designer.
• thermolysis chamber 200 The introduction of the products and the extraction of the residues are thus carried out, in order to avoid the entry of air into the chamber 200, by airlocks which alternately isolate the airlock 100 from the thermolysis chamber 200 when necessary. introduces the products into the airlock 100 and the thermolysis chamber 200 of the cooling chamber 300 when the residues from this third chamber are extracted.
• the thermolysis chamber 200 is insulated to limit heat loss.
• the chamber 200 is maintained at a constant pressure which can be fixed between 200 mbar and 1.2 bar. The same set pressure can be chosen in the other rooms. This pressure is maintained for example by pumping means communicating with the chamber 200 by an extraction line 102, such as a booster described below.
• the gases present in the chamber 200 are aspirated by an extraction line 102 at a temperature, which is in the case of this preferred embodiment, of approximately 330 ° C. They are then passed through a tube heat exchanger 103, as hot fluid.
• This circuit includes a contact cooling means 105, called an oil quench by a person skilled in the art, a pump 106 and a heat exchanger 107.
• the recycling line 104 opens into the cooler 105 from below. this.
• the pump 106 and the heat exchanger 107 are placed on a bypass 104 'of the recycling line 104 which exits from the bottom of the cooler 105 and returns to this cooler 105 from the top.
• a draw-off line 108 for heavy hydrocarbons is connected to this bypass 104 ', between the pump 106 and the exchanger 107.
• the cold fluid of the exchanger 107 is water supplied by the line 109. This water is transformed into steam which comes out through line 110, connected to a steam recovery unit (not shown).
• the gases entering the cooler 105 are cooled by spraying heavy hydrocarbons which have been previously recovered from the bottom of the cooler 105, sucked in by the pump 106, cooled in the heat exchanger 107 to a temperature of approximately 120-130 ° C and reinjected into the cooler 105 from the top of it. Heavy hydrocarbons are thus continuously formed which are partly withdrawn by line 108 and partly recirculated in the cooler 105.
• the uncondensed gases leave the cooler 105 at a temperature of about 150 ° C. and are brought by the recycling line 104 in a condenser 111 intended to cool them down to a temperature of around 45 ° C.
• This condenser 111 is supplied by a refrigerant circulating in a cooling circuit comprising a pump 112 and a fan 113.
• the condensed products accumulate at the bottom of the condenser 111, are extracted from it and introduced into a separator 114 (of the lamellar decanter type), to separate the light hydrocarbons from the water and the organic compounds which are dissolved therein.
• the light hydrocarbons are extracted via line 115 while the aqueous phase is introduced via line 116 into another separator 117, such as a distillation unit, to separate the water from the organic compounds which are dissolved therein.
• the water leaving the separator 117 is brought by a line 118 to a water treatment installation, while the soluble organic compounds leaving this separator 117, by a line 119, can be brought from this line 119 to the boiler 120, to be burned there.
• the uncondensed gases leaving the condenser 111 at a temperature of about 45 ° C are, in turn, brought by the recycling line 104 in a water spraying device 121, also called human water quench of career.
• This device 121 is intended to wash the uncondensed gases in order to rid them in particular of acids, such as hydrochloric acid.
• water is circulated in the device 121, by means of a circuit 122 incorporating a pump 123.
• This circuit 122 includes a bypass 124 allowing the wastewater to be brought to a treatment installation. waters, for example that mentioned above.
• the uncondensed gases leaving the device 121 at a temperature of the order of 45 ° C are, for a first part, reinjected into the heat exchanger 103, via a booster 125 which raises their temperature up to at around 100 ° C.
• This part of gas passes through the heat exchanger 103, as a cold fluid, and leaves it at a temperature of the order of 300 ° C., to then pass through a coil 126 in which the gases of this part of uncondensed gas are heated to a temperature of the order of 650 ° C. by combustion gases from the boiler 120.
• the heated gases enter a line for introducing or supplying hot gases 127 into the chamber 200.
• Another part of the uncondensed gases is brought, via an inlet line 128, to the boiler 120, in which they are burned to heat the part of gas passing through the coil 126.
• the circulation of the gases over this line 128 is provided by a fan 129.
• a third part of these uncondensed gases at low temperature is injected, via an injection line 130, to which a booster 131 is connected, into the cooling zone 300.
• the hot gases recovered from this cooling zone 300 are also recovered on the extraction line 102.
• the hot gases present in the emptying zone 400 are also recovered and introduced into the cooler 105, from the bottom thereof, via a recovery line 132.
• the boiler 120 it will be observed that the combustion gases or fumes produced by the latter are brought by a line 133 to a gas / gas heat exchanger 134 intended to heat the combustion air (air or pure oxygen) used by the boiler 120 and arriving by line 135 entering the heat exchanger 134.
• the boiler 120 is equipped with multi-fuel burners to be able to burn the uncondensed gases but also the light hydrocarbons, the organic compounds dissolved in the water and which have been separated from it or any other liquid or gaseous fuel.
• a fuel line 136 is provided, connected to the boiler
• thermolysis gas storage tank (not shown) can be provided.
• Compression means (not shown) can also be provided to compress the gases before they are stored in the tank.
• pressure and temperature control means are mounted on the various chambers 100 to 400, as well as on the boiler 120.
• means for regulating the gas flow rate by burner at the inlet of boiler 120 are provided at the inlet of this boiler 120.
• the solid residues leaving the cooling zone 300 are treated by wet process in order to separate the mineral fines from the coal.
• the coal can be mixed with the tars recovered in the fractionation train to produce a combustible mixture.
• This combustible mixture could, for example, be burned in the boiler 120 or outside the installation, in particular to produce electrical energy.
• the hot gases introduced into the chamber 200 are enriched, on contact with the charge of solid products to be treated, hydrogen, hydrocarbons (methane, ethane, ethylene), which increases the PCI of these gas (in practice, we go from 4,000 kJ / kg to 18,000 - 19,000 kJ / kg), but also other gases, in particular carbon dioxide, carbon monoxide ...
• the cooling of the gases from the ovens of the thermolysis chamber 200 makes it possible to preserve the pumping means.
• the gases intended to be recycled no longer contain water or tars and the latter can be easily stored or recovered as mentioned above, without fouling the installation.
• the recycling means defined above is here constituted by the coil 126 forming a gas / gas heat exchanger.
• This oven 1 rests on the ground by means of four feet, only three of them being visible in FIGS. 2 and 3 and marked 11 to 13.
• the extraction line 102 opens into the oven 1, through conventional sealing means, from the top of this oven 1 and is extended by a hood 15.
• the latter extends to the immediate vicinity of a carriage 2 and covers the upper end of a tank 16 for receiving solid products, forming part of the carriage 2, the other constituent elements of which will be described in more detail below.
• a hot gas supply line 127 also opens into the furnace 1.
• the sealing of the furnace 1 is here also ensured using conventional sealing means not shown in FIGS. 2 and 3.
• Fluid connection means 20 adapted to establish a temporary fluid connection between the supply line 127 and a connection zone 21 provided on the carriage 2 will now be described.
• These fluid connection means 20 comprise a telescopic device 22, movable between a position for fluid connection of one end of a rigid pipe 23 to the connection area 21 and a position away from the carriage 2.
• the other end of this pipe 23 is, in turn, fluidly connected to the supply line 127.
• the fluid connection means 20 comprise a bellows 24 mounted on the telescopic device 22.
• One end of the bellows 24 is fluidly and sealingly connected to the pipe 23, while its other end provides the temporary fluid connection with the connection zone 21, in the fluid connection position.
• the telescopic device 20 comprises a stirrup 25, the free ends of which are fixed, by screwing, on two opposite sides of a square section frame 26.
• Two tabs 27 extend the stirrup 25 and are pivotally connected, each to one of the two other opposite sides of the frame 26 using means known per se.
• the fixing of the stirrup 25 to the frame 26 and the pivoting connection of the tabs 27 on this same frame 26 is carried out in a substantially median zone on each of the sides of the frame 26 which are connected to each other at their end and across their width.
• each of the legs 27 is integral with a flange or annular part 28 intended to come to be applied on the connection zone 21, by means of a seal 29 made of a material having a certain elasticity and taken in a groove in the annular flange 28.
• One end of the bellows 24 is taken between this flange 28 of a flange 30 screwed onto the flange 28, only one of the screws 31 having been shown in the figures.
• the other end of the bellows 24 is taken between flanges 32 and 33 connecting this second end of the bellows 24 fluidly and sealingly to a frustoconical end of the pipe 23.
• the fixing flanges 32 and 33, one to the other, is carried out using bolt-nut assemblies, only one of which has been shown and identified 34.
• the supply line 127 is in sealed fluid communication with the connection zone 21, in the position of fluid connection of the telescopic device 20.
• the temporary fluid connection can be carried out with a certain flexibility thanks to to the travel possibilities offered by the arrangement thus produced.
• annular seal 28 is also engaged on the first end of the bellows 24.
• the bracket 25 of the telescopic device 20 is actuated by means of a jack of which only the rod 35 has been shown in FIGS. 2 and 3.
• One end of this rod 35 is threaded and passes through an opening made in the base 36 of the stirrup 25 connecting the lateral branches of the stirrup 25 which are fixed to the frame 26.
• the rod 35 abuts by a shoulder against one side of the base 36, while a nut 37 is engaged on the threaded end of the rod 35 and abuts against the other side of the base 36, in order to secure the stirrup 25 to the rod 35.
• the passage of the rod 35 between the inside and the outside of the oven 1 is done through a stuffing box 38 fixed on the underside of the oven 1, also by screwing.
• Means for actuating the rod 35 can be of any type known to a person skilled in the art, such as a pneumatic cylinder, etc. These have not been shown in FIGS. 1 and 2.
• a second bellows 38 ' intended to make the seal, is connected, on the one hand to the base 36 of the stirrup 25 and, on the other hand, to the stuffing box 38, surrounding the rod 35.
• the latter also comprises two beams 39, 40 parallel and of U-shaped cross section each coming, within the furnace 1, to rest in rotation on a row of rollers 41, 42 mounted on consoles 43 , 44 integral with the walls of the oven 1, each by means of a yoke 45, 46 fixed to the console 43, 44 respectively.
• rollers 41, 42 and consoles 43, 44 are of course arranged on either side of the telescopic device 20, so as not to interfere with it.
• the carriage 2 is also guided laterally, on both sides, by means of a plurality of rollers 47, 48 whose mounting is similar to that of the rollers 41, 42, except that they are movable in rotation around of an axis perpendicular to that of the rollers 41, 42.
• Means for moving the carriage 2 outside the oven 1, similar to those which have just been described, or others, can of course be provided outside this oven.
• a plurality of nozzles 49 open out from the bottom of the tank 16.
• the tank 16 is in fact square in shape and consists of four walls of sides 50-53 fixed to each other at their longitudinal ends, here by welding, being walls of sheet metal.
• a tubular system 70 composed, on the one hand, of a central octagonal distributor
• the central distributor 71 comprises two octagonal plates 76, 77 superimposed, in parallel, one on the other, the upper plate 76 being of dimensions slightly smaller than those of the lower plate 77.
• Side walls join the respective parallel sides of the upper 76 and lower 77 octagonal plates and are interconnected by their longitudinal ends.
• each of these side walls is provided with an opening to which is connected the end of a tube, of the type to those marked
• each of these tubes 72, 73 is arranged perpendicular to the corresponding side wall.
• These tube sections 73', 73" have substantially the same length.
• tubes of the type marked 72 and arranged at right angles, also consist of two sections of tube 72 ′, 72 ", of which the one connected to the opening is longer than the second.
• This last section 72" always has a circular section, while the other section 72 'is a flattened tube, connected to the second section 72 "by a tubular element 72" “substantially frustoconical.
• Two sections of tube, of the type marked 74, 75 with circular section are, moreover, fluidly connected to each of the sections of flattened tube 72 ', in the vicinity of the tubular element 72' "and register a right angle.
• the tubular system 70 rests on the angles and the beams, a branch of each of the angles being flush with the corresponding branch of the beam 39, 40 with a U-shaped cross section.
• the central distributor 71 is fixed to the two intermediate angles 63, 64 parallels closest to it, as follows.
• the two parallel side walls of the distributor 71 closest to these angles are provided with a hole for the passage of a nut, while a fixing lug, having a smooth hole aligned with the hole in the side wall, is fixed. , by welding, at the intermediate angle.
• a bolt is engaged in the two aligned holes and a nut is engaged on the free end of the bolt, in the vicinity of the fixing lug, a washer being interposed between the head of the bolt and the side wall.
• the octagonal lower plate 77 of the central distributor 71 has a central circular opening 80.
• the peripheral zone bordering this central opening defines the connection zone 21 mentioned above, the circular opening 80 having substantially the same diameter as the bellows 24 at its free end. It will also be noted that this plate 77 is at the same level as the base of the beams 39, 40 with a U-shaped cross section.
• a nozzle 49 is placed in the vicinity of the closed end of each of the sections of tube 72 ", 73", 74 , 75 having a closed end, near the middle zone of each section of tube 73 'of circular section, on each section of flattened tube 72', at the intersection of sections of tube 74, 75 forming a right angle as well as in the center of the octagonal upper plate 76 of the distributor 71, so as to produce an arrangement of nozzles 49 regularly spaced from one another and covering the entire bottom of the carriage 2.
• the nozzles are screwed by force, with the interposition of a circular wedge 81 on sleeves 82, shouldered outwardly at their base, projecting from the sections of tubes, a free sealing washer 83 being received on the outer peripheral shoulder formed by each sleeve 82.
• nozzles or injectors are provided with calibrated lateral holes (not marked) for the injection of hot gases into the load to be treated and closed at their upper end.
• calibrated lateral holes typically have a diameter of less than a millimeter.
• the bottom of the carriage 2 also comprises a bottom plate 84 (not shown in FIG. 4), such as a sheet metal, drilled at the locations of the sleeves 82, coming to rest on the tubular system 70 and disposed, at the level of the free washers 83, between the latter and the tubular system 70.
• This bottom plate is intended to receive the solid products to be treated.
• this bottom plate 84 is fixed laterally to the peripheral plates 76-79 mentioned above, by means of screws engaged in tapped holes visible in FIG. 3, only two of them carrying the reference 85.
• the other tapped holes of the peripheral dishes 76-79 visible in FIG. 4 are of course identical to those identified. If necessary, lateral wedging stops can be interposed between the screw head and the bottom plate 84.
• the free end of the nozzles 49 is in leaktight fluid connection with the circular opening 80 defined by the connection zone 21 and, consequently, when the telescopic device 20 is in the leaktight fluid connection position, with the hot gas supply line 127.
• a carriage 2 loaded with waste to be treated can be brought to the inlet of the oven 1 and then introduced into it, in rotation on the rollers 41, 42. Then the telescopic device 20 is actuated to bring the seal
• the pumping means are put into action to evacuate the oxygen present in the chamber 200, by the extraction line 102.
• a stream of hot gas is then introduced via the line 127, the pipe 23, the bellows 24, the central distributor 71, the tubular system 70 and the nozzles 49 within the load to be treated, from below, to carry out the dehydration and thermolysis of the solid products.
• the gases from the furnace 1 are then treated as described above in support of FIG. 1.
• the telescopic device 20 is then retracted to allow the carriage 2 to be removed from the oven 1, possibly after cooling.
• a person skilled in the art will also know how to replace the tubular system with a simple pierced grid, for example of calibrated passage holes, constituting an area for receiving solid products to be treated, means of fluid connection being provided to establish a temporary fluid relationship between a hot gas supply line and these through holes.
• the tubular system can also be replaced by a mesh of elements forming passages calibrated to the desired dimensions for a given application.
• the nozzles may also have another shape, such as, for example, a "mushroom" shape, the part facing the receiving area of the carriage is provided with calibrated passages.
• nozzle holes can be replaced by calibrated passages having other shapes, such as slots, for example.
• calibrated passages having other shapes, such as slots, for example.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• Materials Engineering (AREA)
• Organic Chemistry (AREA)
• Combustion & Propulsion (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Processing Of Solid Wastes (AREA)
• Gasification And Melting Of Waste (AREA)
• Physical Or Chemical Processes And Apparatus (AREA)
• Treating Waste Gases (AREA)
• Coke Industry (AREA)
• Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
• Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

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• 1997
  • 1997-10-15 WO PCT/FR1997/001839 patent/WO1998016593A1/fr not_active Application Discontinuation
  • 1997-10-15 WO PCT/FR1997/001838 patent/WO1998016594A1/fr not_active Application Discontinuation
  • 1997-10-15 ES ES97910483T patent/ES2127170T1/es active Pending
  • 1997-10-15 EP EP97910483A patent/EP0879271A1/de not_active Withdrawn
  • 1997-10-15 KR KR1019980704470A patent/KR100282759B1/ko not_active IP Right Cessation
  • 1997-10-15 CA CA002240530A patent/CA2240530A1/fr not_active Abandoned
  • 1997-10-15 BR BR9706864-0A patent/BR9706864A/pt unknown
  • 1997-10-15 JP JP10518072A patent/JP2999558B2/ja not_active Expired - Lifetime
  • 1997-10-15 DE DE0888416T patent/DE888416T1/de active Pending
  • 1997-10-15 BR BR9706834-9A patent/BR9706834A/pt unknown
  • 1997-10-15 US US09/091,302 patent/US6168688B1/en not_active Expired - Fee Related
  • 1997-10-15 EP EP97910484A patent/EP0888416A1/de not_active Withdrawn
  • 1997-10-15 ES ES97910484T patent/ES2127171T1/es active Pending
  • 1997-10-15 JP JP10518073A patent/JPH11504984A/ja active Pending
  • 1997-10-15 CA CA002240532A patent/CA2240532A1/fr not_active Abandoned
  • 1997-10-15 KR KR1019980704471A patent/KR100281312B1/ko not_active IP Right Cessation
  • 1997-10-15 DE DE0879271T patent/DE879271T1/de active Pending
• 2001
  • 2001-04-16 JP JP2001002206U patent/JP3081850U/ja not_active Expired - Lifetime

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