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
  • F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
  • F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
• • 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
  • F23G5/30—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a fluidised bed
• • 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
  • F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
  • F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
  • F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
  • F23G5/165—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber arranged at a different level
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
  • F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
  • F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
  • F23L7/002—Supplying water
  • F23L7/005—Evaporated water; Steam
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
  • F23G2202/00—Combustion
  • F23G2202/10—Combustion in two or more stages
  • F23G2202/101—Combustion in two or more stages with controlled oxidant supply
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
  • F23G2203/00—Furnace arrangements
  • F23G2203/10—Stoker grate furnace
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
  • F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
  • F23L2900/07002—Injecting inert gas, other than steam or evaporated water, into the combustion chambers

Definitions

• the invention relates to a method for the thermal treatment of solids, in particular wastes such as domestic and urban waste, in which the solids are burned / gasified or pyrolyzed in a first stage with a lack of oxygen, and the exhaust gases of the first stage then in a post-combustion chamber with an oxygen-containing gaseous Mixed medium and burned with complete burnout.
• the exhaust gases generated during combustion in and above the bed have a strongly fluctuating composition and temperature in terms of location and time. These exhaust gases are therefore subsequently used in conventional systems of secondary air or secondary air and recirculated flue gas mixed.
• the secondary air fulfills the following functions:
• the primary air added in the first stage is usually sufficient to burn the fuel completely, the secondary air is used to achieve the cross-mixing of the exhaust gas (mixing of CO-containing gas strands with 0 2 -containing gas strands).
• the amount of secondary air blown in must be selected to be correspondingly high. However, this excess of air adversely increases the amount of exhaust gas.
• EP 0 607 210 B1 describes a method for the combustion of solids, in which, in addition to the primary air, no further combustion air is fed into the combustion boiler.
• EP 0 607 210 B1 proposes, on the one hand, to add as much primary air in the first stage that a Excess oxygen results and, on the other hand, water vapor is injected into the combustion boiler above the combustion chamber and in the lower region of the afterburning chamber at a supersonic speed generated by excess pressure.
• This method has the disadvantage that the nitrogen contained in the fuel is oxidized to NO to an increased extent when there is excess air in the first combustion stage, and as a result low NOx emissions cannot be achieved.
• the afterburning chamber was completely separated from the combustion chamber and connected by a pipe.
• the exhaust gas flow was homogenized by turbulence when flowing through this pipe.
• a pipe as a connection between the primary combustion chamber and the afterburning chamber is disadvantageous in the case of a large-scale design (wear and tear).
• the invention tries to avoid these disadvantages. It is based on the object of a process for the thermal treatment of solids, in particular waste, in which the solids are burned / gasified or pyrolyzed in a first stage with a lack of oxygen, and subsequently the escaping gases are mixed with the oxygen-containing medium required for a complete burnout and are burned to develop, eliminating local concentration and temperature fluctuations in the exhaust gas of the first stage and thereby minimizing the pollutant concentrations, in particular the NOx emissions.
• the exhaust gases emerging from the first stage are actively homogenized in a mixing stage with the addition of a gaseous oxygen-free or low-oxygen medium before they are mixed with the oxygen-containing medium and the homogenized oxygen-poor exhaust gas stream emerging from the mixing stage passes through a steady-state zone before the addition of the oxygen-containing medium required for complete burnout, the dwell time in the steady-state zone being at least 0.5 seconds.
• the advantages of the invention are that the gases emerging from the first stage no longer have any concentration and temperature fluctuations due to their subsequent homogenization when they are mixed with the burnout air. Due to the additional residence of the homogenized gas flow in the persistence zone under lack of air (substoichiometric air ratio), the NO already formed can be reduced to N 2 by the NH X , HCN and CO present. As a result, only minimal pollutant emissions occur in the thermal treatment of the solids according to the invention.
• recirculated exhaust gas water vapor, oxygen-depleted air or inert gases such as nitrogen are used as gaseous oxygen-free or low-oxygen media for homogenization.
• gases are advantageously injected into the mixing zone perpendicular to the direction of flow of the exhaust gases or, in order to improve the homogenization and mixing effect, at a certain angle opposite or equal to the direction of flow of the exhaust gases from the first stage.
• the active homogenization of the exhaust gases emerging from the first stage is advantageously carried out by narrowing or widening the cross section of the flow channel.
• the afterburning stage is a fluidized bed and the oxygen-containing gaseous medium is supplied at the entry into the fluidized bed or directly into the fluidized bed.
• the oxygen-containing gaseous medium is supplied at the entry into the fluidized bed or directly into the fluidized bed.
• the steady-state zone is a fluidized bed and the gaseous oxygen-free or low-oxygen medium is supplied at the entry into the fluidized bed or directly into the fluidized bed.
• FIG. 2 shows a partial longitudinal section of a plant for the thermal treatment of waste in a second embodiment of the invention, in which a fluidized bed is used as the first stage;
• FIG. 3 shows a partial longitudinal section of a plant for the thermal treatment of waste in a third embodiment variant of the invention, in which a combustion grate is used as the first stage and a fluidized bed is used as the afterburning zone;
• a combustion grate and a fluidized bed are used as a steady zone
• FIG. 5 shows a partial longitudinal section of a plant analogous to FIG. 3, in which the afterburning zone is a circulating fluidized bed.
• Figure 1 shows schematically part of a plant for the thermal treatment of solids, for. B. garbage or coal in a first embodiment of the invention.
• waste is to be used.
• a grate 2 is arranged in the lower part of a boiler 1, of which only the first train is shown and whose further radiation trains and its convective part are not shown in FIG. 1.
• a medium-current grate combustion is implemented, i. H. the afterburning chamber 14 is arranged in the middle above the grate 2.
• the solids 3, in this case waste, are charged into the boiler 1 and come to rest on the grate 2.
• Primary air 4 is blown through the grate 2 from below. Since only a small proportion of primary air 4 is supplied, only partial combustion or gasification of the waste takes place in this first process stage 5 because of the lack of air or oxygen. It arise in this first 8th
• Stage 5 CO-containing and 0 2 -low exhaust gases 6, which subsequently flow into a mixing zone 7.
• the exhaust gas 6 emerging from the first stage 5 is actively homogenized in this mixing zone 7.
• At least one almost oxygen-free or low-oxygen gaseous medium 8 is added to the mixing zone 7.
• water vapor 9 and, on the other hand, recirculated flue gas 10 are added as medium 8.
• Nitrogen or other inert gases and air with a reduced oxygen content are also suitable for homogenizing the exhaust gas 6 of the first stage 5. It is sufficient if one of these media 8 is introduced into the mixing zone 7, but of course mixtures between these different media 8 are also suitable. 1, the gaseous medium 8 is injected into the mixing zone 7 approximately perpendicular to the flow direction of the exhaust gases 6 in this exemplary embodiment.
• the mixing zone 7 is characterized by changes in the cross section of the walls of the boiler 1, ie changes in the cross section 11 of the flow channel. These cross-sectional changes can be both narrowing and widening of the flow channel.
• the cross-sectional changes 11 support the exhaust gas homogenization.
• additional internals 12 are arranged in the mixing zone 7, which ensure a flow deflection of the exhaust gases 6 and thus further mixing and active homogenization of the exhaust gases 6.
• the static mixer 12 have cavities (not shown in the figure), which with coolant, for. B. air, water or water vapor.
• the homogenized CO-rich exhaust gas emerging from the mixing zone 7 then passes into a steady-state zone 13 in which there is also a lack of oxygen, that is to say a substoichiometric air ratio is present.
• a steady-state zone 13 part of the NO already formed from the furnace is reduced to N 2 in the presence of CO, NH, and HCN.
• the residence time of the homogenized exhaust gases in the steady-state zone 13 is at least 0.5 seconds. At a normal exhaust gas velocity of approximately 4 m / s, this means that the steady-state zone must be at least approximately 2 m long.
• the exhaust gas then flows from the steady-state zone into the post-combustion stage 14. There, an oxygen-containing medium 15, for example air (secondary air), is mixed in, so that a complete burnout of the exhaust gas is ensured.
• an oxygen-containing medium for example air (secondary air)
• the process according to the invention for the graded thermal treatment of solids is characterized by simple process steps and by a 10
• FIG. 2 shows a further exemplary embodiment of the invention, which differs from the first exemplary embodiment only in that a fluidized bed 16 is used instead of the combustion grate in the first process stage 5.
• the waste 3 is burned sub-stoichiometrically in the fluidized bed 16, a very good material and heat exchange advantageously taking place and local temperature peaks being prevented.
• the mixing and homogenization of the gas 6 emerging from the fluidized bed 16 (first stage 5) also takes place, as in the first exemplary embodiment, in the subsequent mixing zone 7, into which a gaseous, virtually oxygen-free or low-oxygen medium 8, for. B.
• FIG. 3 shows an exemplary embodiment in which, in contrast to the example shown in FIG. 1, the afterburning zone 14 is designed as a fluidized bed 16.
• the oxygen-containing gaseous medium 15 is introduced either directly into the fluidized bed 16 or at the inlet into the fluidized bed 16. These two alternatives are shown in FIG. 3.
• the afterburning zone 14 as a fluidized bed 16
• local hot zones with high thermal NOx formation are avoided due to the increased heat transfer due to the presence of particles.
• caking on heat exchanger walls can be prevented and corrosion on heat exchanger surfaces can be considerably reduced.
• Higher steam pressures and temperatures can also be set, which enable a higher thermal efficiency of the incineration plant.
• FIG. 4 shows a partial longitudinal section of a plant for the thermal treatment of waste in a fourth embodiment variant of the invention, in which a combustion grate 2 is used as the first stage and a fluidized bed 16 is used as the persistence zone 13.
• the mixing zone 7 in this exemplary embodiment is characterized by a cross-sectional expansion.
• an intensive material and heat exchange then advantageously takes place in the fluidized bed 16 (steady-state zone 13). 12
• FIG. 5 shows a further embodiment variant, which differs from FIG. 3 only in that the fluidized bed 16 in the afterburning stage 14 is a circulating fluidized bed in which the empty pipe speed in the riser pipe is increased.
• the fluidized material is discharged into a cyclone and then returned to the fluidized bed.
• the average vertical gas velocity in the riser pipe is higher than in the classic fluidized bed, and the average relative velocity between gas and particles also increases. This leads to an increased heat and mass exchange between gas and particles and thus to a reduced temperature and concentration distribution.
• the amount of heat removed from the fluidized bed can be varied and the fluidized bed temperature and the temperature at the end of the afterburning zone can be set well.
• the invention is not limited to the exemplary embodiments described.
• the steady-state zone 13 can also be designed as a circulating fluidized bed or a grate system with countercurrent firing is used.
• Boiler rust solids e.g. B. Waste primary air first process stage exhaust gas from item 5 mixing zone oxygen-free or low-oxygen gaseous medium water vapor recirculated exhaust gas cross-sectional changes of the flow channel internals / static mixer steady-state post-combustion stage oxygen-containing gaseous medium fluid bed

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• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• General Engineering & Computer Science (AREA)
• Chemical & Material Sciences (AREA)
• Combustion & Propulsion (AREA)
• Incineration Of Waste (AREA)
• Fluidized-Bed Combustion And Resonant Combustion (AREA)

Priority Applications (1)

Applications Claiming Priority (6)

Publications (1)

Family

ID=26151922

Family Applications (1)

Country Status (8)

Families Citing this family (18)

Family Cites Families (19)

• 1999
  • 1999-05-10 CN CN998060348A patent/CN1218141C/zh not_active Expired - Lifetime
  • 1999-05-10 US US09/700,163 patent/US6336415B1/en not_active Expired - Fee Related
  • 1999-05-10 WO PCT/CH1999/000192 patent/WO1999058902A1/de active IP Right Grant
  • 1999-05-10 KR KR1020007012562A patent/KR100549654B1/ko not_active IP Right Cessation
  • 1999-05-10 JP JP2000548664A patent/JP2002514732A/ja active Pending
  • 1999-05-10 HU HU0102798A patent/HUP0102798A3/hu unknown
  • 1999-05-10 EP EP99917726A patent/EP1078203A1/de not_active Ceased
  • 1999-05-10 CA CA002332011A patent/CA2332011A1/en not_active Abandoned

Non-Patent Citations (1)

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