JP2012037186A - Incineration apparatus of high moisture content waste - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide an apparatus for efficiently incinerating a high moisture content waste containing a solid and moisture.SOLUTION: An incineration apparatus includes: a fragmentation device for fragmenting a solid of a waste containing the solid and moisture; a spray device for spraying an incineration target containing the fragmented solid; a guiding means for guiding the sprayed incineration target containing the solid to an incineration site in an atomized state while floating the incineration target in the air; and a combustion device such as a pulse combustion device or a heating device which is provided on the incineration site, comprises e.g., a combustion chamber, a fuel supplying device for supplying a fuel to the combustion chamber, and an ignition device which explodes the fuel together with air, introduces the atomized incineration target into the combustion chamber together with the fuel and the air, incinerates the incineration target with combustion heat generated by repeating the explosion, and exhausts the gas.

Description

  The present invention relates to an incinerator for high water content waste.

  When processing organic waste, which is industrial waste, such as shochu lees or manure (such waste has a high moisture content, and generally has a moisture content of 90% or more) Techniques for incinerating them have been proposed in the following patent documents.

JP 09-234457 A

  In this treatment method, pulsed combustion gas (high temperature exhaust gas) discharged downward from a pulse combustor is combusted, for example, by bringing manure, septic tank sludge, or a mixture thereof into contact with each other to form dry powder and water vapor. is there.

  However, this pulse combustion drying apparatus has poor combustion efficiency for manure or sludge in a septic tank, and requires considerable fuel consumption by pulse combustion.

  An object of the present invention is to provide an incinerator for waste having a high water content, which has a high combustion efficiency and requires little fuel.

Means for Solving the Problems and Effects of the Invention

In order to solve the above problems, the high moisture content waste incineration apparatus of the present invention is an apparatus for incinerating waste containing solids and moisture,
A fragmentation device for fragmenting the solid,
A spraying device for spraying the incineration object containing the subdivided solids;
Guidance means for guiding the sprayed incinerator containing the solid matter to the incineration place in an atomized state while floating in the air;
A combustion device or a heating device which is provided at the incineration place and incinerates the incineration object;
It is characterized by providing.

  In this way, the incineration object containing solids is atomized together with moisture, and the incineration object is incinerated and exhausted, so that the combustion efficiency is very high, and therefore fuel can be reduced. Is also easy.

  Further, in the present invention, the guiding means is provided between a place where the spraying device is installed and the incineration place, and promotes or maintains the atomization state of the incineration target, and a lower part of the flow chamber. And an ascending fan or an air jet part that raises the incineration object while preventing the incineration object from descending to the bottom of the fluid chamber.

  Thereby, it can be guide | induced to a combustion place, maintaining or promoting the atomization state of incineration object.

In the present invention, the guiding means includes a plurality of flow chambers provided between the installation location of the spraying device and the incineration location for promoting or maintaining the atomization state of the incineration target, and the flow chambers. An ascending fan or an air ejection part that is provided at least at one lower part and prevents the incineration object from descending to the bottom of the fluidized chamber and raises the incineration object;
A duct communicating with the plurality of flow chambers;
A transfer fan or an air injection unit that is provided at a boundary portion of the fluid chamber and the duct or in the middle of the duct and sends the atomized incineration object to the incineration site side;
including.

  In this way, the atomization of the incineration object is maintained or promoted by the ascending fan or the air ejection part in the fluid chamber, and in that state, it can be guided to another fluid chamber or an incineration place via the duct.

  Moreover, in this invention, in the said flow chamber which forms the immediate space where the said incineration object is sprayed by the said spraying apparatus, it is a mist among the incineration objects on the opposing wall facing the side to which the incineration object is sprayed. An adhering member for adhering the incineration object that remains as a fluid without being converted into a fluid is provided, and a temporary storage unit that collects the incineration object in the form of the fluid is disposed below the adhering member, and In the temporary storage part, there is located an air jet part for spraying the fluid-like incineration object temporarily stored in the temporary storage part as it is or added to the space with compressed air and atomizing it.

  In this way, the incineration object that is not atomized may remain in a fluid state in the state immediately after the incineration object is sprayed by the spray device, but in that case, the incineration object is provided on the opposing wall to be sprayed. The fluid-like incineration object is temporarily attached to the adhering member, and is guided so as to flow downward, and is stored in the temporary storage part, where the fluid-like incineration object is compressed by the compressed air ejected from the air ejection part. Can be atomized. This makes it possible to forcibly perform atomization again on the upstream side where residues that cannot be atomized easily remain, and prevent the incineration target from being accumulated downward in the fluid chamber.

  Further, in the present invention, the rising fan is provided close to the lower side of the air ejection portion in the flow chamber, and the damper for changing the rising angle of the air flow by at least one of the rising fan and the air ejection portion is changed in angle. Installed as possible.

  In this way, the rising angle of the airflow for re-atomization can be adjusted, so that the rising angle can be adjusted according to the amount of residue that could not be atomized. Contributes to atomization.

  In the present invention, an example of the combustion device includes a combustion chamber, a fuel supply device that supplies fuel to the combustion chamber, and an ignition device that explodes the fuel together with air, and the atomization into the combustion chamber A pulse combustion apparatus that incinerates the incineration object in the combustion chamber and exhausts the incineration object with combustion heat generated by introducing the incineration object together with the fuel and air and repeating explosions. According to this combustion apparatus, since the atomized incineration object is incinerated in the combustion chamber of the pulse combustion apparatus by the combustion heat accompanying the explosion, the combustion efficiency is extremely high. Further, since it is possible to substantially leave only the exhaust so that almost no visible combustion residue is generated, post-processing is easy.

  Further, another example of the combustion apparatus of the present invention includes a combustion chamber for allowing the atomized incineration object to flow, and a flame radiating section for radiating a flame into the combustion chamber, and the incineration is performed by the combustion heat of the flame. A burner that incinerates the subject. Also by this, the atomized incineration object can be introduced and this can be incinerated effectively.

  An example of the heating device of the present invention includes a heating chamber into which the incineration object is allowed to flow, and a heating source provided in the vicinity of the heating chamber, and the incineration object is heated by the heat of the heating source in the heating chamber. It is a heating furnace to be incinerated. The atomized incineration object is incinerated by heat in a high temperature heating chamber of the heating furnace.

The whole schematic diagram of the incinerator of the high moisture content waste of the present invention. Schematic which shows the fragmentation apparatus and spraying apparatus of the upstream of FIG. Schematic which shows from the upstream in FIG. 1 to a 1st flow chamber. Schematic which shows to the 2nd flow chamber and 3rd flow chamber in FIG. Schematic which shows to the 4th fluidization chamber and incineration chamber in FIG. The longitudinal cross-sectional view which expanded the re-atomization apparatus in the 1st fluidization chamber of FIG. The perspective view which shows the principal part of the air ejection part for the re-atomization. The typical top view of the air ejection part of FIG. Action | operation explanatory drawing of the damper in the lower side of the re-atomization apparatus of FIG. The simple longitudinal cross-sectional view which shows an example of the pulse combustion apparatus in the incinerator of FIG. The conceptual diagram which shows the vertical incinerator which is another Example of this invention. The conceptual diagram corresponding to FIG. 11 which shows another Example which increased the partition wall in FIG. The plane conceptual diagram which shows the other example of an injection apparatus. The conceptual diagram which expands and shows the part of the injection nozzle of FIG. The simplified sectional view showing an example of a burner type combustion device as a combustion device. The simplified sectional view showing an example of the heating furnace type heating device which incinerates the incineration object.

  Hereinafter, embodiments of the present invention will be described based on examples shown in the drawings.

  FIG. 1 shows an overall view of a waste incineration apparatus according to the present invention in the form of a simplified longitudinal sectional view. This incinerator 1 is an incineration object W such as shochu lees that contain solid matter such as dietary fiber and has a considerably high water content (eg, water content of 80% or more), or livestock or human feces and urine containing solid matter such as feces. Is incinerated by a pulse combustion device in an atomized state.

  First, on the upstream side, which is the left end of FIG. 1, a subdividing device 2 for subdividing the solid content of the incineration object W, and a spraying device 3 for spraying the incineration object W containing the subdivided solid matter are provided. The immediately sprayed room is the first flow chamber 4, the second flow chamber 5 downstream thereof, the third flow chamber 6 and the fourth flow chamber 7 are located, and pulse combustion is performed in the most downstream incineration chamber 8. The device 13 is located. Further, a duct 10 that connects the first fluid chamber 4 and the third fluid chamber 6, a duct 11 that interconnects (communicates) the second fluid chamber 5 and the third fluid chamber 6, the third fluid chamber 6 and the fourth fluid chamber. 7 is provided with a duct 12 connecting (communicating) 7. A re-atomizing device 14 to be described later is provided on the opposing wall of the first fluid chamber 4 facing the spray device 3, and an ascending fan for raising the incineration target W below the first fluid chamber 4. 17 is provided together with the damper 41, a rising fan 18 is also provided below the third flow chamber 6, and a rising fan 19 is also provided below the fourth flow chamber 7, and the second flow chamber 5 and the duct 10 are further provided. The ascending fan 21 is also arranged at the boundary portion between.

  Moreover, the transfer fan 22 which sends the incineration object W in the atomized state to the incineration place (incineration chamber 8) is at the boundary between the first flow chamber 4 and the duct 10, and a similar transfer fan 23 is the second. A transfer fan 24 is provided at the boundary between the flow chamber 5 and the duct 11, a boundary between the third flow chamber 6 and the duct 12, and a transfer fan at the downstream end of the fourth flow chamber 7 immediately before the incineration chamber 8. 25 are arranged. The incineration object W sprayed by the spray device 3 on the upstream side is promoted or maintained in an atomized state in the first fluid chamber 4, the second fluid chamber 5, the third fluid chamber 6, and the fourth fluid chamber 7, respectively. It is transferred to the pulse combustion device 13 side of the incineration chamber 8 by the transfer fans 22, 23, 24, 25 through the ducts 10, 11, 12. Note that, at the boundary between the first fluid chamber 4 and the second fluid chamber 5, an air ejection portion 40 is provided as a part of the re-atomizer 14 for the incinerator W, and the bottom corner of the second fluid chamber 5 is provided. The air ejection part 20 is further provided at the boundary between the duct 10 and the third flow chamber 6, and these functions promote or maintain the atomization of the incineration object W by the ejection of the pressure air, and The transfer function to the combustion chamber 8 is achieved.

  In the following, the structure from the upstream side toward the downstream side shown in FIG. FIG. 2 shows the upstream portion in FIG. 1 and shows the incineration object W until it is sprayed by the spraying device 3 after being subdivided by the subdividing device 31. In this example, for example, an electric mill or the like can be adopted as the subdividing device 31, and the incineration object W such as the shochu and solid waste containing the solid content is input from the hopper 70, For example, the incineration object W subdivided into 100 to 500 mesh is stored in the storage tank 71. The incineration target W in this state is a fluid having a moisture content of 90% or more, for example, and is sent by the pump 27 to the injection nozzle 30 of the incineration target W through the supply pipe 29 provided with the valve 28. On the other hand, the compressed air compressed by the compressor 32 is sent to the air jetting part 34 through the pipe line 33, where the incineration object W is sprayed, in other words, atomized by the principle of spraying. The space to be atomized is the first fluid chamber 4.

  FIG. 3 is a view up to the first fluid chamber 4 (spray chamber). The incineration object W is sprayed into the first fluid chamber 4 by the spray device 3 and floats in the space, and is further sent downstream through the duct 10 by the transfer fan 22, but not all are atomized. In some cases, some of the liquid does not atomize and adheres in droplets to the inner surface of the boundary wall 36 with the adjacent second flow chamber 5. Here, on the boundary wall 36, a guide member 37 (for example, one in which a wave pattern is arranged vertically) formed with a plurality of downward grooves for guiding the attached droplets downward, and a net member 38 on the inner side thereof are provided. A part of the incineration object W that is disposed and sprayed from the spraying device 3 adheres to the mesh member 38 (attachment member) or the guide member 37 facing in the spraying direction and hangs downward, so that a bowl-like temporary storage is performed. Stored in the part 39. The temporary storage section 39 has an air ejection section 40, and the incineration object W as a liquid fluid stored in the temporary storage section 39 is re-atomized by the pressure air ejected therefrom. The re-atomizer 14 includes these members 37, 38, 39 and 40.

  The ascending fan 17 is located below the temporary storage unit 39, and the damper 41 is located directly downstream thereof. When the specific gravity of the incineration target W is large, the damper 41 is adjusted to have a large inclination angle in order to blow it higher. When the specific gravity of the incineration target W is small, the damper 41 is manually or electrically adjusted to such an extent that the inclination angle is small. Adjusted by mechanism.

  6 and 7 show the re-atomizing device 14 in an enlarged manner. The air ejection part 40 is formed by forming air ejection holes 40b and 40c in a supply pipe 40a for supplying pressure air, for example, and the pressure air supplied here is ejected from the air ejection holes 40b and 40c. As a result, the incineration object W, which is a liquid fluid stored in the bowl-shaped temporary storage unit 39 in FIG. In FIG. 6, the net member 38 prevents the incineration object W adhering thereto from becoming a liquid film, and promotes it to drop and drop down. A guide member 37 (a corrugated tin or the like) located adjacent to it makes it easy for the droplets to sag downward.

  FIG. 8 is a schematic diagram in plan view of the air ejection part 40. As shown in the figure, the ejection holes and the like are set so that the left and right ejection paths collide with each other, and the droplets or mists collide with each other. Further atomization of the incineration target W is promoted. FIG. 9 illustrates the operation of the above-described damper 41. The inclination angle is increased so that the incineration object W rises as much as possible when the specific gravity is large. That's enough.

  FIG. 4 shows portions of the second flow chamber 5 and the third flow chamber 6 that are further downstream from the first flow chamber 4. The incineration object W atomized again in the second fluid chamber 5 is sucked up by the transfer fan 21 provided in the upper part of the second fluid chamber 5 and flows into the duct 10, and the upper side surface of the second fluid chamber 5. It is divided into that which flows into the duct 11 by the transfer fan 23. Moreover, the mist-like incineration object W which is going to descend | fall to this corner | angular part by the air ejection part 40 provided in the corner | angular part of the lower part (bottom face) of the 2nd fluidization chamber 5 is raised upwards. At the lower part of the third fluid chamber 6 located next to the second fluid chamber 5, there is an ascending fan 18 that blows up the mist-like incineration object W flowing into the interior through the ducts 10 and 11, and is raised by this. The incineration object W merges with the one flowing in from the duct 10 at the upper end of the third fluid chamber 6, and further descends after exceeding the upper end of the vertical partition wall 6a (the upper part is open). Then, it is sent to the duct 12 side by the transfer fan 24. Thus, what flows in from the duct 11 of the incineration object W is raised in the third fluid chamber 6 and merges with what comes from the duct 10 so that they are entirely lowered to the transfer fan 24 side. The crystallization state is promoted or maintained. 26 is an air ejection part, which plays the same role as the transfer fan.

  FIG. 5 shows the fourth flow chamber 7 and the incineration chamber 8 located further downstream of the third flow chamber 6. The incineration object W is sent to the fourth fluid chamber 7 from the lower region through the duct 12 in the form of a mist, and the incineration object W is moved to the fourth fluid chamber 7 by the rotation of the rising fan 18 provided in the lower part of the fourth fluid chamber 7. The transfer fan 24 is driven so as to be blown up toward the upper part of the four flow chambers 7 and over the partition wall 7a (the upper part is open) partitioning the fourth flow chambers 7 and to descend again. Further, the mist-like incineration object W flows into the most downstream incineration chamber 8 through a flow of lowering. The incineration chamber 8 has the above-described pulse combustion device 13, which is a so-called pulse jet engine. When an explosion of fuel (for example, kerosene) occurs in the incineration chamber (for example, the combustion cylinder), the rest A pulse-like explosion is continuously maintained at a constant cycle.

  FIG. 10 shows the pulse combustion apparatus 13 in the incineration chamber 8 more specifically. The pulse combustion apparatus 13 includes a pipe member 51 having flanges at both ends, an end plate 50 fixed to the opening on the inlet side, and a combustion chamber 62 ( And a housing 52 that constitutes a combustion chamber 68 (second) following the first). This main body is further accommodated in the case 53, and the case 53 is installed on the floor surface of the incineration chamber 8 via the installation unit 69. The end plate 50 is formed with an intake port 57 for taking in air. Air is sucked into the combustion chamber 62 from the intake port 57, and the above-described incineration object W in the form of mist is burned together with the air into the combustion chamber 62. Flows in. Further, the end plate 50 is provided with a fuel injection nozzle 58, and fuel such as kerosene is supplied to the fuel injection nozzle 58 from a fuel tank 60 through a conduit 59 by a pump 61. At 58, fuel is injected into the combustion chamber 62.

  A spark plug 63 is arranged in the vicinity, and the first explosion is performed by the spark plug 63. However, the ignition of the spark plug 63 is not required due to the features of the pulse jet engine. Will continue. The blast and explosion heat are generated in the first combustion chamber 62, and a guide portion 65 that receives the impact of the explosion is provided in a state fixed to the housing 52. The guide portion 65 is, for example, a triangular pyramid-shaped umbrella, and is supported by the fixing portion 65b via the plurality of support portions 65a in a state where the outer periphery is spaced apart from the housing 52 by a certain distance. This triangular pyramid-shaped guide portion 65 prevents the blast and heat of explosion from flowing directly from the first combustion chamber 62 into the second incineration chamber 68, and from the center side to the outer peripheral side with respect to the inflow direction. It is located so as to gradually move away from the injection nozzle 58. The blast is spread widely to the outer peripheral side by the guide portion 65 and then flows into the combustion chamber 68 through the outer edge of the guide portion 65. This effectively increases the temperature of the combustion chamber 62 and the combustion chamber 68.

  The pulse combustion device 13 is a water-cooled type, and a pipe member 67 through which cooling water is passed is disposed in an incineration chamber 68 in a predetermined form, and cooling water is supplied to the pipe member 67 to generate heat. The deprived hot water is drained to the outside. Further, in this example, the combustion chamber 68 is provided with an exhaust port 66 in a direction substantially perpendicular to the inflow direction of the air and the mist-like incineration object W, and this exhaust port 66 is disposed in the combustion chamber 68 and is further predetermined. It is escaped outside by the route of.

  In the combustion chamber 62 of such a pulse combustion device 13, the incineration object W containing the fine solid matter that has been atomized as described above flows together with the air, and is caused by the explosion of fuel injected from the fuel injection nozzle 58. The first combustion chamber 62 and the second combustion chamber 68 following the first combustion chamber 62 are incinerated. Thereafter, only mere exhaust is exhausted from the exhaust port 66. Therefore, there is substantially no combustion residue, the post-treatment is simple, and the conventional idea of burning in the combustion chamber 62 (inside) and the combustion chamber 68 of the pulse combustion apparatus 13 is, for example, burned by a burner. Are completely different, have good combustion efficiency, and can eliminate the incineration target with little fuel and no trace.

  The pulse combustion apparatus described above is merely an example, and a combustion apparatus using various pulse combustion apparatuses can be employed. For example, a mist-like incineration target and a pulse combustion device in which the inflow direction and the exhaust direction of air are coaxial may be provided, or a partition member having a large number of holes may be provided instead of the guide portion 65. Moreover, it does not necessarily need to be water-cooled, and may be air-cooled.

  Furthermore, in the above description, the case where there are four flow chambers 4, 5, 6, 7 from the first to the fourth is taken as an example, but this is also an example only, and the simplest one is as follows: An incineration chamber having a pulse combustion device may be adjacent to the first fluidization chamber. Further, the re-atomization device 14 provided on the facing wall for the injection of the first fluid chamber may be omitted when the atomization is good. Further, when there are a plurality of fluid chambers, they are connected by a duct, but the duct may be omitted and the fluid chambers may be connected to each other through the opening of the partition wall.

  In the above embodiment, the incineration target atomized from the upstream spray position is guided horizontally toward the downstream incineration place (it can be said that the atomization proceeds in the process), but the vertical type or tower shown in FIG. A mold incinerator 80 may be used. In this incinerator 80, the incinerated object is sprayed upward in the housing 81 by the spray device 83 (basic structure is the same as the spray device 3 in FIG. 1 and the like) and blown up thereabove. The mist-like incinerator is lowered from the upper part by the partition wall 82 whose upper part is released, and is atomized with respect to the combustion device 85 (for example, the pulse combustion device of FIG. 10) located at the incineration place set in the lowered part. Incinerated objects are introduced and incinerated here. Fans 86, 87, etc., are provided as needed to send the combustion target to the incineration site.

  In addition, as shown in FIG. 13, the injection device 83 includes an air injection pipe 96 for injecting pressure air and a combustion target injection pipe 95 for injecting an incineration target whose solid content is subdivided, respectively. Each of the pipes 95 and 96 is formed with a pair of injection ports 97 and 98 which are close to each other, and the incineration object is fogged by the pressure air and the incineration object injected from each pair of injection ports 97 and 98. It is blown up into a shape.

  In this case, as shown in FIG. 14, the extension line between the pressure air injection port 97 and the combustion target injection port 98 intersects, in other words, the pressure air from the injection port 97 and the incineration target from the injection port. Can incline the formation axis of the injection ports 97 and 98 so that they collide at a predetermined angle after injection (collision with each other), thereby efficiently atomizing the object to be incinerated. Promoted.

  Next, the incinerator 90 shown in FIG. 12 is provided with a plurality of partition walls 82 (in this case, two) for partitioning the housing 91 by opening the upper part thereof, and the injection device 83 moves upward as compared with the incinerator 90 shown in FIG. The sprayed mist-like incinerator is repeatedly raised, lowered, raised and lowered, and finally flows into the combustion device 92 where it is incinerated. Again, if necessary, an appropriate number of fans 86 for sending the mist-like incineration object to the combustion site side, and a rising fan 93 (for the fan) that blows the mist-like incineration object upward to maintain or promote the atomization. Alternatively, an air ejection part may be provided.

  In the above description, the pulse combustion apparatus is typically exemplified to incinerate the mist-like incineration object, but a so-called burner can be employed instead. A combustion apparatus 92 shown in FIG. 15 includes a burner unit 100 that radiates a flame toward an atomized passage to be combusted in a burner housing 99, to which combustion gas or the like is supplied from a fuel source 101, and from there. The mist-like incineration object is burned and extinguished in the combustion chamber (99) by the generated flame. For combustion of the burner unit 100, an ignition device 102 and an exhaust device 103 such as a fan for promoting exhaust are provided.

  Furthermore, instead of a combustion device such as a pulse combustion device or a burner, an incinerator by heating can be used. For example, the heating device 104 shown in FIG. 16 is a so-called heating furnace (kiln), the inside of the main body 105 is a heating chamber 107, and a heating coil 106 (a heating source such as a burner) provided in the vicinity of the main body 105 may be used. ), The heating chamber 107 is heated to a high temperature of, for example, about 1000 to 1400 ° C., and the mist-like combustion object flowing into (introducing) the heating chamber 107 is incinerated at the high temperature. Here, an exhaust passage 108 for exhaust, a fan 109 for promoting exhaust, and the like can be added as appropriate.

DESCRIPTION OF SYMBOLS 1 Incineration apparatus of high moisture content waste 2 Subdivision apparatus 3,83 Spray apparatus 4 1st fluidization chamber 5 2nd fluidization chamber 6 3rd fluidization chamber 7 4th fluidization chamber 8 Incineration chamber 10,11,12 Duct 17,18 , 19, 21 Ascending fan 22, 23, 24, 25 Transfer fan 20, 26, 40 Air ejection portion 58 Fuel injection nozzle 62 Combustion chamber 65 Guide portion 66 Exhaust port 68 Incineration chamber 85, 92 Combustion device 104 Heating device

Claims (8)

An apparatus for incinerating high water content waste containing solids and moisture,
A fragmentation device for fragmenting the solid,
A spraying device for spraying the incineration object containing the subdivided solids;
Guidance means for guiding the sprayed incinerator containing the solid matter to the incineration place in an atomized state while floating in the air;
A combustion device or a heating device which is provided at the incineration place and incinerates the atomized incineration object;
An incinerator for high moisture content waste, comprising:   The guide means is provided between a place where the spraying device is installed and the incineration place, and is provided in a flow chamber for promoting or maintaining the atomization state of the incineration target, and a lower portion of the flow chamber, and the incineration The incinerator for high moisture content waste according to claim 1, further comprising an ascending fan or an air ejection part that raises the incineration object while preventing the object from descending to the bottom of the fluidized chamber. The guiding means includes a plurality of flow chambers provided between the installation place of the spraying device and the incineration place for promoting or maintaining the atomization state of the incineration target, and at least one lower part of the flow chambers. An ascending fan or an air ejection unit for raising the incineration object by preventing the incineration object from descending to the bottom of the fluid chamber;
A duct communicating with the plurality of flow chambers;
A transfer fan or an air injection unit that is provided at a boundary portion of the fluid chamber and the duct or in the middle of the duct and sends the atomized incineration object to the incineration site side;
A high water content waste incinerator according to claim 1.   In the flow chamber that forms the immediate space in which the incineration object is sprayed by the spraying device, the fluid that is not atomized in the incineration object is opposed to the opposite wall that faces the side to which the incineration object is sprayed. An attachment member for adhering the remaining incineration object to flow downward is provided, and a temporary storage part for collecting the fluid-like incineration object is disposed below the attachment member, and further, in the temporary storage part The high water content disposal according to claim 2 or 3, wherein an air ejection part is disposed in which the incineration object in the form of a fluid temporarily stored therein is scattered as it is or added to the space with compressed air and atomized. Incineration equipment.   The rising fan is provided close to the lower side of the air ejection part in the flow chamber, and a damper for changing the rising angle of the airflow by at least one of the ascending fan and the air ejection part is installed so that the angle can be changed. The incinerator for high water content waste according to any one of claims 2 to 4.   The combustion device includes a combustion chamber, a fuel supply device that supplies fuel to the combustion chamber, and an ignition device that explodes the fuel together with air, and the atomized incineration object into the combustion chamber, The incinerator for high moisture content waste according to claim 1, wherein the incinerator is a pulse combustion apparatus that incinerates and incinerates the incineration object in the combustion chamber by combustion heat that is introduced together with the fuel and air and repeats explosion.   The combustion apparatus is a burner that includes a combustion chamber that allows the atomized incineration target to flow in, and a flame radiating unit that radiates a flame into the combustion chamber, and incinerates the incineration target with the combustion heat of the flame. Item 2. An incinerator for high moisture content waste according to item 1.   The heating apparatus includes a heating chamber into which the incineration target is allowed to flow and a heating source provided in the vicinity of the heating chamber, and the incineration target is incinerated by heat of the heating source in the heating chamber. The high moisture content waste incinerator described.

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