Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
  • F23C10/00—Fluidised bed combustion apparatus
  • F23C10/02—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed
  • F23C10/04—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone
  • F23C10/08—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases
  • F23C10/10—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases the separation apparatus being located outside the combustion chamber
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
  • B01J8/0025—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor by an ascending fluid
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/005—Separating solid material from the gas/liquid stream
  • B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
  • B01J8/1836—Heating and cooling the reactor
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
  • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
  • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
  • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
  • B01J8/388—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
  • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
  • C10J3/46—Gasification of granular or pulverulent flues in suspension
  • C10J3/48—Apparatus; Plants
  • C10J3/50—Fuel charging devices
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
  • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
  • C10J3/46—Gasification of granular or pulverulent flues in suspension
  • C10J3/54—Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
  • C10J3/56—Apparatus; Plants
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
  • F23C10/00—Fluidised bed combustion apparatus
  • F23C10/18—Details; Accessories
  • F23C10/24—Devices for removal of material from the bed
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
  • F23C10/00—Fluidised bed combustion apparatus
  • F23C10/18—Details; Accessories
  • F23C10/28—Control devices specially adapted for fluidised bed, combustion apparatus
  • F23C10/30—Control devices specially adapted for fluidised bed, combustion apparatus for controlling the level of the bed or the amount of material in the bed
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F27—FURNACES; KILNS; OVENS; RETORTS
  • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
  • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
  • F27B15/02—Details, accessories, or equipment peculiar to furnaces of these types
  • F27B15/10—Arrangements of air or gas supply devices
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
  • B01J2208/00008—Controlling the process
  • B01J2208/00017—Controlling the temperature
  • B01J2208/00106—Controlling the temperature by indirect heat exchange
  • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
  • B01J2208/00743—Feeding or discharging of solids
  • B01J2208/00761—Discharging
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
  • C10J2300/00—Details of gasification processes
  • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
  • C10J2300/1693—Integration of gasification processes with another plant or parts within the plant with storage facilities for intermediate, feed and/or product
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
  • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
  • C10J3/46—Gasification of granular or pulverulent flues in suspension
  • C10J3/48—Apparatus; Plants
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
  • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
  • C10J3/46—Gasification of granular or pulverulent flues in suspension
  • C10J3/48—Apparatus; Plants
  • C10J3/52—Ash-removing devices

Definitions

• the present invention relates to a treatment system in accordance with the preamble of claim 1 for removing bed material of a fluidized bed reactor from the fluidized bed reactor and for cooling the bed material to be removed.
• the treatment system comprises a treatment chamber in connection with the fluidized bed reactor, which treatment chamber is provided with means for sup- plying fluidizing gas to the lower portion of the treatment chamber, a heat exchanger system arranged in an internal space formed by the treatment chamber, feeding arrangement for bed material, opening to the treatment chamber and being in connection with the fluidized bed reactor; and a first discharge connection arranged in the bottom portion of the treatment chamber for remov- ing cooled bed material from the treatment chamber.
• the present invention also relates to a method in accordance with the preamble of claim 9 of removing bed material of the fluidized bed reactor from the fluidized bed reactor and of cooling the bed material to be removed, in which method bed material is transferred to a treatment system in connection with the fluidized bed reactor, in which system the bed material to be treated is fluidized by supplying fluidizing gas to the lower portion of the treatment chamber; transferring heat from the bed material by means of a heat exchanger system which is arranged in an internal space formed of the treatment chamber; guiding bed material from the fluidized bed reactor by means of a feeding arrangement in connection with the fluidized bed reactor and opening to the treatment chamber; and removing cooled bed material by a first discharge connection through a bottom portion of the treatment chamber out of the treatment chamber.
• the fluidized bed reactor is an apparatus known as such for accomplishing different reactions and treatment processes.
• a characteristic feature of a fluidized bed reactor is a fluidized bed, which is formed by conducting an ap-rank
• the reaction medium and the possible additives form substance that is coarser in the grain size, which must in practice be removed from the fluidized bed reactor. Such a substance is generally called bottom ash.
• the fluidizing velocity is so high that a portion of the solid material is entrained with the reaction and/or fluidizing gas
• the particles of the external circulation are, however, typically relatively small of the grain size.
• Publication EP 0062092 B1 discloses a cooling apparatus for the bottom ash of the fluidized bed reactor and a method, in which the cooler is used in different manners.
• bed material can be transferred to the cooler of the bottom ash determined by the drive mode of the reactor.
• So called stripper-cooler type external heat exchangers are also bottom ash removal arrangements known in the prior art, in which the ash to be removed is transferred through one or more fluidizing chambers, in which it cools down and, on the other hand, the finer ash fraction is recirculated with the flui- dizing gas back to the furnace.
• a problem with these solutions is that the mass flow and the grain size of the solid material flowing in cannot be controlled, which causes clogging and problems in the temperature control. Complicated structure and large size can also be considered problematic in these solutions.
• Publication US 4969404 discloses a cooling system for bottom ash, in which the bottom ash to be removed from the reactor is fluidized in such a way that the lighter material is separated from the bottom ash and supplied with the fluidizing gas back to the reactor, when heavier material is removed. In the disclosed arrangement, there is no possibility to control the size of the bottom ash flowing into the system, so it can easily clog, if too large particles are allowed in.
• Publication US 4227488 discloses a principally similar bottom ash cooler with a difference that it also discloses a heat exchanger arranged into the cooler. For this reason, this solution has even a bigger risk to clog.
• Publication US 7240639 B2 discloses a fluidized bed heat exchanger arranged in connection with a fast fluidized bed reactor, through which heat exchanger bed material of the fluidized bed reactor is recirculated and cooled down prior to the return of the bed material to the fast fluidized bed reactor.
• bed material is supplied to the fluidized bed heat exchanger to a level which is to a certain extent above the grid of the fast fluidized bed reactor so as to avoid the entrance of larger particles possibly in the bottom of the fast fluidized bed reactor to the fluidized bed heat exchanger.
• Publication WO 9620782 A1 also discloses a bottom ash cooler arranged in connection with a fast fluidized bed reactor.
• the cooler is arranged to operate in two stages, in which the first stage is for separating and removing a coarser solids portion from the bottom ash by fluidizing appropriate- ly and transferring the finer solids portion to the second stage. Only at the second stage solids portion is cooled by fluidizing the solids portion in a space comprising a heat exchanger.
• the publication also discloses a second alternative for realization, in which a special route formed of slots or holes, in which the slots/holes prevent the transfer of particles that are larger than the predetermined size from the reactor to the ash cooler.
• Publication EP 0 700 316 B1 discloses an apparatus for processing bed material of the fluidized bed reactor, in which bed material is removed from the fluidized bed reactor and transferred to a higher level in the process chamber by means of a special lifting chamber.
• the publication discloses a flow path formed of special slots or holes between the fluidized bed reactor and the lifting chamber, in which slots/holes prevent the transfer of particles of larger than the predetermined size from the reactor to the lift chamber.
• the publication discloses the removal of such larger particles from the lifting chamber, which are not transferred with the fluidizing gas to the processing chamber.
• a disadvantage in such an arrangement is, for example, a risk of clogging the slots/holes.
• An object of the invention is to provide a treatment system for removing bed material of the fluidized bed reactor from the fluidized bed reactor and cooling said bed material, which enables better than before the control in the removal of the bed material and a more reliable operation.
• Another object of the invention is to provide a method of removing bed material of a fluidized bed reactor from the fluidized bed reactor and cooling it.
• a treatment system for remov- ing bed material of the fluidized bed reactor from the fluidized bed reactor and for cooling the bed material to be removed, said treatment system comprising a treatment chamber in connection with the fluidized bed reactor, which treatment chamber is provided with means for supplying the fluidizing gas to the lower portion of the treatment chamber; a heat exchanger system, which is arranged to an internal space formed by the treatment chamber; a feeding arrangement for bed material, which on one hand opens to the treatment chamber and on the other hand is in connection with the fluidized bed reactor; a first discharge connection arranged to the bottom portion of the treatment chamber for removing cooled bed material from the treatment chamber.
• the feeding arrangement opens at least through two different inlet openings to different horizontal levels in the reaction chamber of the fluidized bed reactor.
• in operational proximity of said two inlet openings there are means for guiding the flow of the bed material from the fluidized bed reactor to the treatment chamber that are independent from the fluidization of the fluidized bed reactor.
• in operational proximity of said at least two inlet openings there are independently controllable means for controlling the flow of the bed material from the fluidized bed reactor to the treatment chamber.
• the feeding arrangement of the bed material is formed of at least two separate feed channels, which each have a separate inlet opening and feed opening, through which bed material can be transferred from the reaction chamber to the treatment chamber.
• inlet openings through which bed material is supplied to the treatment chamber, open to the treatment chamber substantially at the same horizontal level, which is above the heat exchanger system of the treatment chamber.
• At least one inlet opening of the feeding arrangement of the bed material opens to the reaction chamber substantially to the level of the grid thereof.
• the means for supplying the fluidiz- ing gas to the lower portion of the treatment chamber comprise a grid structure, arranged vertically at a lower lever than the grid structure.
• the treatment chamber and the reaction chamber are preferably provided with a common wall portion, in which said feeding arrangement for bed material is arranged.
• the objects of the invention are also achieved by means of a method of removing bed material of a fluidized bed reactor from the fluidized bed reactor and cooling the bed material of the fluidized bed reactor, in which method bed material is transferred to a treatment system in connection with a fluidized bed reactor, in which system the bed material to be treated is fluidized by supplying fluidizing gas to the lower portion of the treatment chamber; transferring heat from the bed material by means of a heat exchange arrangement, which is arranged to an internal space formed by a treatment chamber; guiding bed material from the fluidized bed reactor by means of a feeding arrangement which is in connection with a fluidized bed reactor and opens to the treatment chamber; and removing cooled bed material by means of a first discharge connection through a bottom portion of the treatment chamber from the treatment chamber. It is characteristic to the invention that bed material is transferred to the treatment chamber from the fluidized bed reactor at least at two locations arranged at different horizontal levels.
• the transfer of bed material at said two different locations is controlled by independently guiding the flow of the bed material from the fluidized bed reactor to the treatment chamber. [0023] The transfer of the bed material at two different locations is controlled by locally affecting the fluidization of the bed material.
• the fluidization of the bed material is locally affected in such a way that the transfer of particles having a grain size and/or weight less than a set value is allowed.
• inlet flow of the bed material to the treatment system can be controlled, also batch mode possible
• thermal energy content of the bed material to be removed is efficiently recovered
• FIG. 1 schematically illustrates an embodiment of a treatment system of the bed material of a fluidized bed reactor
• Fig. 2 illustrates a section ll-ll of Fig. 1 .
• Fig. 1 illustrates a preferred embodiment of the invention of a treatment system 20 arranged in connection with a fluidized bed reactor 10 for removing bed material of a fluidized bed reactor from the fluidized bed reactor.
• the system can especially be used for efficiently controlling the amount of the bed material to be removed and grain size thereof.
• the fluidized bed reactor 10 is preferably a fast fluidized bed reactor, in other words a circulating fluidized bed reactor for combusting or gasifying fuel.
• the main elements of a circulating fluidized bed reactor are a reaction chamber 12, which is called a furnace in combustion applications, a solids separator system 14 and a solids recirculating system 16.
• the solids separator system preferably comprises one or more eye- lone separators arranged to separate bed material, in other words solid material entrained with gases from the furnace.
• the separated solid material is recirculated completely or partially through the recirculation system 16 back to the furnace.
• feed means 1 1 for fluidizing gas in the bottom portion of the reaction chamber which comprise at least a so called wind box 1 1 .1 , a grid 1 1 .2 and control means 1 1 .3 arranged in the channel leading gas to the wind box for controlling the flow rate of the fluidizing gas.
• the bottom portion of the reaction chamber also contains a discharge connection 17 for removing particularly large particles formed of the bed material.
• a treatment system 20 is provided in connection with the lower portion of the reactor, which system preferably operates as fluidized bed cooler 20, in which unburned substances of the bed material removed from the reaction chamber are treated.
• the cooler 20 and the treatment chamber 24 thereof are preferably provided with a wall portion 22 common with the reaction chamber 12.
• a treatment system in accordance with the invention is arranged in connection with the fluidized bed reactor 10 for removing a desired portion of the bed material.
• the treatment system 20 comprises a treatment chamber 24, provided with means 26 for introducing the fluidizing gas to the lower portion of the treatment chamber 24, whereby the treatment system comprises a fluidized bed cooler 21.
• the means 26 for supplying fluidizing gas preferably comprise a bottom portion provided with gas inlet openings and gas supplying device 30 provided with control means 28.
• Means 26 of the treatment chamber 24 for supplying fluidizing gas to the lower portion of the treatment chamber comprise a grid structure 30.1 provided with gas nozzles, which are preferably provided ⁇
• a first discharge connection 32 is provided at the level of the bottom portion of the treatment chamber 24, for removing cooled bed material from the treatment chamber 24.
• the first discharge connection 32 is provided with a control means 31 for removing the bed material in such a manner that the gas flow through the discharge connection is substantially prevented or diminished at the same time.
• the control means can be, for example, a rotary valve feeder or like.
• a discharge connection 32 is preferably connected to a screw conveyor 46, by means of which the cooled solid material is transferred to be further treated.
• the temperature of the bed material to be removed at the bottom of the cooler is considerably lower than the bed temperature of the furnace 12, whereby owing to the invention the temperature of the bed material to be removed does not considerably limit the capacity of the screw(s) to be used.
• a heat exchange system 34 is provided in the treatment chamber, which system comprises heat exchange surfaces arranged in connection with the bed material.
• the heat exchange surfaces are arranged, while the apparatus is running, below the surface of the fluidized bed to be formed in the treatment chamber.
• heat is recovered from the bed material to be removed and cooled down before guiding it to the discharge connection 32.
• the treatment system 20 also comprises a second discharge connection 34, which is arranged to the upper portion of the treatment chamber to connect a gas space of the treatment chamber to the reaction chamber 12. It is possible to remove the fluidizing gas supplied to the treatment chamber through the second discharge connection 34 to the reaction chamber 12.
• the second discharge connection 34 is arranged in such a manner that it is not possible to transfer considerable amounts of bed material from the reaction chamber 12 to the treatment chamber 24.
• the treatment system 20 comprises feeding arrangement 36 for bed material, by means of which it is possible to remove a controlled amount of material with a controlled grain size from the furnace 12.
• the feeding arrangement 36 is in connection with the reaction chamber 12 of the fluidized bed reactor ⁇ cca
• a feed channel 42 connects the inlet opening and the feed opening.
• the feed opening 40 is at a higher horizontal level than the inlet opening 38, whereby the bed material does not flow nor transfer from the reaction chamber 12 to the treatment chamber by itself practically at all.
• the feed channel 42 delimits such a space that the fluidization of the furnace 12 alone does not enable the transfer of the bed material through the inlet channel to the treatment chamber 24.
• Independently controlled means 44 for guiding the flow of the bed material from the fluidized bed reactor to the inlet opening 38 and through the inlet opening to the treatment chamber 24 are provided in the close operational proximity of the inlet opening 38 to the inlet opening 38 in order to generate the flow of the bed material and the transfer of the bed material from the reaction chamber 12 to the treatment chamber.
• the means 44 for guiding the flow of the bed material from the fluidized bed reactor to the treatment chamber comprise an inlet arrangement for fluidizing gas arranged substantially at the inlet opening in such a way that the fluidizing gas to be supplied can be adjusted independently from the supply of the fluidizing gas of the reaction chamber.
• Said inlet arrangement of the fluidizing gas is preferably arranged in such a way that the fluidizing gas to be supplied therethrough is guided to the inlet channel and flows therethrough to the treatment chamber 24.
• Such a feeding arrangement 36 enables the possibility to control by means of the amount of the fluidization both the amount of the bed material to be transferred and the grain size thereof.
• There the inlet opening 38 does not operate as primary means to determine the grain size of the bed material, so the inlet opening can be so large that the risk of clogging is avoided practically speaking completely.
• the furnace comprises a discharge connection 17 for the removal of the possible oversized agglomerates.
• means 26 of a fluidized bed cooler 20 for supplying fluidizing gas to the lower portion of the treatment chamber 24 is in connection with a discharge gas channel 9 of the ⁇ ⁇
• fluidized bed reactor 10 When the reactor is a combustion device, gas, which does not contain oxygen, and which is available in the reactor is used as fluidiz- ing gas. This provides that the possibly combustible portion of the bed material to be cooled does not burn, whereby the cooling continues to be efficient. Also other non-oxygenous gas can be used, if desired, as fluidizing gas of the treatment system.
• the fluidized bed cooler shown in Fig. 1 will be run in batch mode. There, at the first stage the inlet arrangement 44 for the fluidizing gas is switched on, whereby material is transferred from the proximity of the inlet opening 38 through the inlet channel 42 to an upper level and through the inlet opening 40 to the treatment chamber 24. The grain size of the transferred material is controlled by the fluidizing velocity. This will be continued until there is a desired amount of cooled bed material in the treatment chamber.
• the feed of the fluidizing gas is started by means of the means 26 for supplying fluidizing gas to the lower portion of the treatment chamber 24. Simultaneously heat is recovered from the bed material removed from the reaction chamber by means of heat exchanger system 34 and the bed material is cooled. When the temperature of the bed material has decreased to the pre-determined temperature, cooled bed material batch is removed through the discharge connection 32.
• Fig. 2 discloses a partial section ll-ll of Fig. 1 , which illustrates a detail of an embodiment in accordance with a preferred embodiment.
• the Figure illustrates a wall of a reaction chamber 12 and a feeding arrangement 36 of the treatment system 20 in connection therewith.
• the feeding arrangement 36 of the bed material opens through at least two, here through three different inlet openings 38, 38', 38" to the fluidized bed reactor 10.
• Each inlet opening is arranged to a controlled reception of bed material from the reaction chamber 12 in such a manner that the operation thereof is independent from the fluidization of the reaction chamber.
• the inlet opening 38 operates as flow path to the inlet channel 42, which further leads through the inlet opening 40 at the upper end thereof to the treatment chamber 24.
• the grid structure 30.1 of the treatment chamber of the treatment system is at the lower level than the grid structure 1 1 .2 of the reaction chamber 12 of the fluidized bed reactor 10.
• Fig. 2 illustrates three different inlet openings 38, 38', 38" and they are located at different levels in regard to the grid 1 1.2 of the reaction chamber. The lowermost thereof is substantially at the level of the grid 1 1 .2 of the reaction chamber.
• the horizontal distance of the inlet openings from each other is pre- ferably such that the independent operation of each inlet opening is possible especially as for the supply 44 of the fluidizing gas.
• the inlet openings 38, 38', 38" may be different from their surface areas depending, for example, on the vertical location of the portion to be removed in the fluidized bed of the reaction chamber.
• each inlet opening comprises fluidizing means 44 for the control of the flow of the bed material from the fluidized bed reactor to the treatment chamber, which means 44 can be individually controlled.
• fluidizing means 44 for the control of the flow of the bed material from the fluidized bed reactor to the treatment chamber, which means 44 can be individually controlled.
• the apparatus illustrated in Figs. 1 and 2 is used in such a way that bed material is transferred to a treatment system 20 in connection with the fluidized bed reactor, in which it is fluidized by supplying fluidizing gas 26 to the lower portion of the treatment chamber.
• the fluidizing gas is non-oxygenous gas.
• a slow fluidized bed is maintained in the treatment chamber, the upper surface of which is arranged above the heat exchanger system 34 and to which heat exchanger system heat is transferred from the bed material.
• Bed material is guided by a feeding arrangement opening to the treatment chamber and being in connection with the fluidized bed reactor from the fluidized bed reactor 20 from a location arranged at least at two different horizontal levels.
• the feeding arrangement can comprise inlet openings the number of which deviates from the embodiment shown in the Figure. Some of them may also be at the same vertical distance from the grid 1 1 .2. In some cases, more than one inlet opening and/or feed opening can be connected to the same inlet channel 42.
• the medium used in the heat exchange arrangement 34 is preferably low temperature medium, for example, feed water or a separate water circuit, through which heat is transferred, for example, to combustion air. -.
• the pipe distribution of the heat exchanger is sparse enough to enable the easy access of coarser material to the bottom of the chamber, too.
• the treatment system in accordance with the invention can also be applied in connection with an existing fluidized bed reactor, whereby it is also possible to utilize the existing appropriate treatment chamber. Thereby, it is needed to form at least a feeding arrangement for the bed material to the wall between the treatment chamber and reaction chamber or in connection therewith in such a manner that the feeding arrangement opens through at least two different inlet openings 38, 38', 38" to different horizontal levels in the reaction chamber 12 of the fluidized bed reactor.
• the treatment chamber is provided, if such do not yet exist, with means 26 for supplying fluidizing gas to the lower portion of the treatment chamber 24; a heat exchanger system 34 to the internal space formed by the treatment chamber; and a discharge connection 32 for the discharge gases of the treatment chamber. Otherwise, the treatment system will be formed as described above. [0049] It must be noted that only some most preferred embodiments of the invention are described above. Thus, it is obvious that the invention is not limited to the above described embodiments, but it may be applied in many ways. The features disclosed in connection with different embodiments can also be used with other embodiments within the basic concept of the invention and/or it is possible to form different combinations of the features illustrated, if such is desired and is technically feasible.

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• Oil, Petroleum & Natural Gas (AREA)
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Citations (4)

• 2010
  • 2010-09-23 FI FI20105979A patent/FI20105979A0/fi not_active Application Discontinuation
• 2011
  • 2011-09-21 WO PCT/FI2011/050808 patent/WO2012038598A1/en active Application Filing

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