[go: up one dir, main page]

WO2018124261A1 - Incinérateur - Google Patents

Incinérateur Download PDF

Info

Publication number
WO2018124261A1
WO2018124261A1 PCT/JP2017/047167 JP2017047167W WO2018124261A1 WO 2018124261 A1 WO2018124261 A1 WO 2018124261A1 JP 2017047167 W JP2017047167 W JP 2017047167W WO 2018124261 A1 WO2018124261 A1 WO 2018124261A1
Authority
WO
WIPO (PCT)
Prior art keywords
combustion chamber
rooster
incinerated
incinerator
air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2017/047167
Other languages
English (en)
Japanese (ja)
Inventor
強 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Alphacorporation Co Ltd
Kaisho Co Ltd
Original Assignee
Alphacorporation Co Ltd
Kaisho Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Alphacorporation Co Ltd, Kaisho Co Ltd filed Critical Alphacorporation Co Ltd
Publication of WO2018124261A1 publication Critical patent/WO2018124261A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/38Multi-hearth arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories

Definitions

  • the present invention relates to an incinerator that incinerates various incinerated materials at a high temperature, and more particularly to an incinerator that is optimal for incineration of bamboo.
  • the incinerator completely incinerates the incinerated materials to incinerate them without leaving unburned materials, reducing the incineration ash, and clarifying exhaust gas without generating various harmful substances such as bad odor, dust, and dioxin. It is important to do. This can be achieved by raising the combustion temperature. Various incinerators have been developed to achieve this. (See Patent Document 1)
  • the incinerator of Patent Document 1 is provided with a rooster 87 that rotates at the bottom of the primary combustion chamber, a projecting portion is provided at the center of the rooster 87, and air is provided around the projecting portion. A blowing outlet is provided. Further, in this incinerator, a secondary combustion chamber is provided in an exhaust pipe connected to the upper side of the primary combustion chamber, and a burner is connected thereto. The above incinerator supplies the incinerated product to the rotating rooster 87, and air is supplied to the rooster from the protrusion provided in the center.
  • Combustion gas generated by combustion in a rooster rotating in the primary combustion chamber flows into a secondary combustion chamber provided in an exhaust pipe connected to the primary combustion chamber, and is discharged after secondary combustion.
  • incinerator incinerator is supplied to the rotating rooster and burned, the combustion gas generated here is raised, burned in the secondary combustion chamber provided in the exhaust pipe, and discharged to the outside.
  • the structure becomes extremely complicated.
  • the above incinerators rotate the rooster in the combustion chamber in an extremely harsh external environment.
  • the rooster is rotated in the primary combustion chamber, the rooster is rotated stably over a long period of time. It is difficult to burn in a favorable state.
  • it is difficult to increase the combustion temperature in the primary combustion chamber because the high-temperature combustion gas generated in the primary combustion chamber naturally flows into the secondary combustion chamber and is difficult to stay in the primary combustion chamber. .
  • the present invention was developed for the purpose of solving the above drawbacks.
  • An important object of the present invention is to incinerate the incinerated products at an extremely high temperature while minimizing unburned substances and incinerated ash as much as possible, and to generate various harmful substances such as foul odors, dust and dioxins.
  • An object of the present invention is to provide an incinerator capable of clarifying exhaust gas by reducing the amount.
  • the incinerator of the present invention includes a primary combustion chamber 1 and a secondary combustion chamber 2 into which combustion gas flows from the primary combustion chamber 1, and supplies the incinerated material to the primary combustion chamber 1 to generate combustion gas. It is discharged outside through the next combustion chamber 2. Further, the incinerator has all the following configurations A to J.
  • An incinerated supply port 3 is opened above the primary combustion chamber 1, a secondary combustion chamber 2 is disposed below the primary combustion chamber 1, and the primary combustion chamber 1 and the secondary combustion chamber 2 are separated from each other by a partition plate 4. It is divided up and down.
  • the supply port 3 is connected to a feeder 5 that supplies the incinerated product while blocking the discharge of combustion gas and the inflow of air. C.
  • the partition plate 4 opens a gas flow path 6 through which the combustion gas in the primary combustion chamber 1 flows into the secondary combustion chamber 2.
  • a rooster 7 is arranged on the partition plate 4 at the supply position of the incinerated product to be introduced from the supply port 3.
  • the primary combustion chamber 1 is connected to a blower 8 that forcibly blows air toward the rooster 7.
  • the rooster 7 includes a plurality of multi-stage plates 9 that are stacked in multiple stages on the partition plate 4 via the air blowing gaps 11.
  • the multistage plate 9 includes an uppermost multistage plate 9A arranged at the uppermost stage, and a lower multistage plate 9B arranged in multistage below the uppermost multistage plate 9A. H.
  • the uppermost multi-stage plate 9 ⁇ / b> A has uppermost inclined plates 10 ⁇ / b> A that are inclined downward toward the outside on both sides of the top edge extending in the blowing direction of the blower 8.
  • the lower multi-stage plate 9B has a lower inclined plate 10B that protrudes outside the uppermost inclined plate 10A and is inclined downward toward the outside.
  • the blower 8 blows air toward the rooster 7 and blows it to the outside from the blow gap 11 between the multi-stage plates 9 stacked in multiple stages.
  • the above incinerators have an extremely simple structure, incinerate the incinerated products at extremely high temperatures to minimize unburned substances and incinerated ash, and reduce the generation of various harmful substances such as foul odors, dust and dioxins. It has the feature that exhaust gas can be clarified by decreasing. This is because the above-mentioned incinerator uses the unique structure of the rooster 7 to incinerate the incinerated product in an ideal state with the combustion gas flow in an ideal state.
  • the unique structure of the rooster 7 provided in the incinerator of the present invention includes a plurality of multi-stage plates 9, a plurality of multi-stage plates 9 arranged in multiple stages, and a ventilation gap 11 provided between the upper and lower sides.
  • the uppermost multi-stage plate 9A arranged at the top has a tapered shape in which the lateral width is gradually narrowed from one end to the other end, the top edge is a mountain shape that slopes downward, and inclined plates 10A are provided on both sides of the top edge.
  • the inclined plate 10A is shaped to be inclined downward from the top edge toward the side edges on both sides, and the lower multi-stage plate 9B disposed below the uppermost multi-stage plate 9A is An inclined plate 10B protruding outside the upper inclined plate 10A is provided, and the inclined plate 10B is also inclined in a downward gradient toward the outside.
  • Incinerators are supplied to the rooster 7 from the supply port 3 while preventing the inflow of air.
  • the rooster 7 is an inclined plate 10 in which air blown from the blower 8 to one end is arranged in multiple stages.
  • Combustion exhausted from the primary combustion chamber 1 by disposing a secondary combustion chamber 2 that blows outside from the air gap 11 between them and discharges the combustion gas in the primary combustion chamber 1 below the primary combustion chamber 1 Realize the feature of incineration of incinerated products at high temperatures by limiting gas emissions.
  • the incinerator described above supplies the incinerated material to the rooster 7 and incinerates it, but the incinerated material supplied to the rooster 7 is incinerated while sliding down the inclined plate 10, but on the inclined plate 10 of the rooster 7.
  • the incinerated product to be incinerated is incinerated while falling through the air gap 11 between the inclined plates 10 arranged in multiple stages, but since the air gap 11 is blown from the air from the inside, the incinerator falling here Since the objects fall while being replenished with oxygen in a state of being dispersed, they are incinerated in an ideal state.
  • the inclined plate 10 heated to a high temperature heats the incinerated product to be supplied, evaporates and vaporizes water contained in the incinerated material, decomposes the vaporized water, generates hydrogen, and burns hydrogen.
  • the combustion temperature is further increased to incinerate the incinerated material at a high temperature.
  • the incinerator prototyped by the present inventor succeeded in setting the temperature of the combustion gas in the primary combustion chamber 1 to an extremely high temperature of 1310 ° C.
  • An incinerator capable of treating incinerated materials at this temperature has very few unburned substances and incinerated ash, and has a feature that exhaust gas can be extremely clarified with almost no generation of various harmful substances such as bad odor, dust and dioxin.
  • the incinerator of the present invention when bamboo is incinerated in the incinerator of the present invention, the amount of incinerated ash generated is extremely small, and the feature of limiting the amount of inorganic precipitates to be deposited is also realized.
  • bamboo is incinerated with a conventional incinerator, a large amount of inorganic material contained in the bamboo adheres to the inner surface, making it impossible to incinerate over a long period of time, but the incinerator of the present invention incinerates at an extremely high temperature. Therefore, since there is almost no deposit of inorganic deposits and the amount of incinerated ash generated is extremely small, the characteristics of incineration of bamboo over a long period of time are realized.
  • the incinerator of the present invention can adjust the flow rate and flow rate of the air forcedly blown by the blower 8 by adjusting the power supplied to the motor of the blower 8 by the inverter 12.
  • the incinerator described above has a feature that the incinerated material can be incinerated in an ideal state by adjusting the flow velocity of air forcedly blown by the inverter 12 to an optimum value.
  • the uppermost multi-stage plate 9A has a tapered shape in which the lateral width is gradually narrowed in the air blowing direction, and the top edge is inclined downward in the air blowing direction. It can be.
  • This incinerator is characterized in that the incinerated product supplied to the rooster 7 can be dispersed and dropped on both sides and forward and efficiently incinerated.
  • the partition plate 4 of the incinerator of the present invention can open the gas flow path 6 on both sides of the rooster 7.
  • the incineration ash incinerated by the rooster 7 can be dispersed on both sides and smoothly dropped into the secondary combustion chamber 2.
  • the combustion gas gasified by the rooster 7 can smoothly flow into the secondary combustion chamber 2 to efficiently perform secondary combustion.
  • the incinerator of the present invention can have a structure in which a plurality of roosters 7 are arranged on the partition plate 4 and the incinerated products are incinerated by forcibly blowing air to each rooster 7.
  • This incinerator can incinerate a large amount of incinerators with a plurality of roosters 7 per unit time.
  • the incinerator of the present invention opens the gas flow path 6 along the side edge of the rooster 7 so that the combustion gas burned in the rooster 7 can flow into the secondary combustion chamber 2 more smoothly.
  • the inclined plates 10 of the lower multi-stage plate 9B can be arranged in a V shape, and the inclined plates 10 on both sides can be arranged on both sides of the rooster 7.
  • the inside of 7 is made into a cavity, and the air forcedly blown here is sent to the outside uniformly from the multistage air gaps 11, and the incinerated product can be efficiently incinerated.
  • FIG. 3 It is sectional drawing of the longitudinal direction of the incinerator concerning the Example of this invention. It is a horizontal sectional view of the II line of FIG. FIG. 3 is a vertical sectional view taken along line III in FIG. 1. It is a side view of the rooster arrange
  • the incinerator of the present invention is not intended to be used for incineration of incinerated products, but also includes those used for the purpose of effectively using thermal energy generated by incinerating various incinerated products. Used for.
  • An incinerator shown in FIGS. 1 to 3 includes a primary combustion chamber 1, a secondary combustion chamber 2 into which combustion gas flows from the primary combustion chamber 1, a rooster 7 disposed in the primary combustion chamber 1, and a rooster 7 And a blower 8 that forcibly blows air toward.
  • the primary combustion chamber 1 is disposed on the secondary combustion chamber 2, and the primary combustion chamber 1 and the secondary combustion chamber 2 are partitioned vertically by a partition plate 4.
  • the partition plate 4 is disposed in a horizontal posture, and the partition plate 4 has a primary combustion chamber 1 above and a secondary combustion chamber 2 below.
  • the partition plate 4 opens a gas flow path 6 through which combustion gas flows from the primary combustion chamber 1 to the secondary combustion chamber 2.
  • the partition plate 4 in FIG. 2 has triangular gas flow paths 6 opened at the corners and the center on both sides.
  • the gas flow path 6 is opened along both sides of the rooster 7 arranged in two rows, and the combustion gas of the incinerated product supplied to the rooster 7 is forcibly flowed from the top to the bottom to form the secondary combustion chamber.
  • Incinerated ash formed on the rooster 7 is also dropped into the secondary combustion chamber 2.
  • the gas flow path 6 opened close to both sides of the rooster 7 causes the incinerated ash that is incinerated while falling on both sides of the rooster 7 to smoothly fall into the secondary combustion chamber 2.
  • the primary combustion chamber 1 has a supply port 3 for incinerated materials on the ceiling.
  • the supply port 3 is directly above the rooster 7, and the incinerated product supplied from the supply port 3 is dropped onto the rooster 7.
  • the supply port 3 is supplied with the incinerator from a feeder 5 that supplies the incinerated product while blocking the discharge of the combustion gas and the inflow of air.
  • the feeder 5 of FIG. 3 is connected in the middle of the supply pipe connected to the supply port 3.
  • the feeder 5 shown in the figure includes two shutters 13 that are horizontally reciprocated in the middle of the supply pipe, an actuator 14 that reciprocates each shutter 13 separately, and a reciprocation of the actuator 14. And a controller 15 for controlling movement.
  • the controller 15 alternately reciprocates the two shutters 13 with the actuator 14 to supply the incinerated material to the primary combustion chamber 1 from the supply port 3.
  • the controller 15 opens the upper shutter 13 in a state where the lower shutter 13 is closed, and supplies the incinerated material onto the lower shutter 13. Thereafter, with the upper shutter 13 closed, the lower shutter 13 is opened, and the incinerated product is dropped into the primary combustion chamber 1. After supplying the incinerated product to the primary combustion chamber 1, the lower shutter 13 is closed and the upper shutter 13 is opened, and the operation of supplying the incinerated product to the lower shutter 13 is repeated, and the incinerated product is primarily burned from the supply port 3. Drop into chamber 1.
  • the above feeder 5 controls the actuator 14 with the controller 15 and adjusts the timing at which the actuator 14 alternately opens and closes the shutter 13 up and down to control the supply amount of the incinerated products.
  • the above feeder 5 alternately opens and closes the two shutters 13 to supply the incinerated material to the primary combustion chamber 1.
  • the present invention does not specify the feeder 5 as the above structure, for example, a rotary feeder. Anything that can supply the incinerated product to the primary combustion chamber while shutting off the outflow of combustion gas and the supply of air can be used.
  • Incinerator is supplied to the feeder 5 via a conveyor such as a screw conveyor.
  • the controller 15 controls the conveyor and the feeder 5 to adjust the supply amount of the incinerated product.
  • the incinerators shown in FIGS. 1 to 3 are arranged with two rows of roosters 7 on the partition plate 4, and gas passages 6 are opened on both sides of each rooster 7.
  • the supplied combustion gas and incineration ash are dropped from the gas flow path 6 to the secondary combustion chamber 2.
  • FIG. 4 is a side view of the rooster 7
  • FIG. 5 is a plan view of the rooster 7
  • FIG. 6 is a perspective view of the rooster 7 as viewed from the upper back, and FIG.
  • the rooster 7 shown in these figures is installed on the partition plate 4.
  • the rooster 7 includes a plurality of multi-stage plates 9 stacked in multiple stages via the air blowing gap 11.
  • the multi-stage plate 9 is provided with a blowing gap 11 by connecting both ends of the rear end and the three ends of the front end with connecting bars so that the forcedly blown air can flow smoothly.
  • interval of the ventilation gap 11 is set to the optimal value by the kind and magnitude
  • the interval of the air blowing gap 11 is preferably about 2 cm to 5 cm.
  • the illustrated rooster 7 has a rear-end air gap 11 wide and a front-end air gap 11 gradually narrowed so that the uppermost multi-stage plate 9A is inclined downward toward the front end.
  • the air gap 11 is set to an optimum value depending on the type and size of the incinerated material, and is, for example, 1 cm or more, preferably 1.5 cm or more, more preferably 2 cm or more, preferably 10 cm or less, more preferably 6 cm. The following range can be adjusted to the optimum range. Further, the air gap 11 can be set smaller or larger than the above range depending on the type and size of the incinerated product, and can be set to a value at which the incinerated product can be incinerated in an ideal state.
  • the multistage plate 9 includes an uppermost multistage plate 9A and a lower multistage plate 9B arranged in multiple stages below the uppermost multistage plate 9A.
  • the uppermost multistage plate 9 ⁇ / b> A is provided with uppermost inclined plates 10 ⁇ / b> A that are inclined downward toward the outside on both sides of the top edge 16 extending in the blowing direction of the blower 8.
  • the inclination angle ( ⁇ ) at which the inclined plate 10A is inclined downward toward the outside is set to about 45 degrees with respect to the horizontal plane.
  • the inclined plate 10 having this inclination angle can be incinerated at a high temperature while sliding down in an ideal state using bamboo as an incinerator.
  • the inclination angle ( ⁇ ) specifies the staying time of the incinerated material.
  • the time for which the incinerated material stays on the inclined plate 10 is set so as to slide down in a state where the incinerated material is incinerated to become incinerated ash. If the inclination angle ( ⁇ ) is too large, the staying time is shortened and slips down from the inclined plate 10 in a state where it is not sufficiently incinerated. Conversely, if the inclination angle ( ⁇ ) is too small, the staying time becomes long and the incineration ash is smoothened. Can no longer slide down.
  • the inclination angle ( ⁇ ) of the uppermost inclined plate 10A is set to an optimum value in consideration of the physical properties of the supplied incinerated material, and is set to be larger than 15 degrees and smaller than 60 degrees, for example. .
  • the inclined plate 10 having a large inclination angle ( ⁇ ) is suitable for supplying a non-slip incinerated product and incineration in a preferable state, and the inclined plate 10 having a small inclination angle ( ⁇ ) incinerate a slippery incinerated product. Suitable for
  • the uppermost multi-stage plate 9A shown in FIG. 5 has a tapered shape in which the lateral width is gradually narrowed in the air blowing direction, and the top edge 16 is inclined in a downward gradient in the blowing direction.
  • the top edge 16 of the uppermost multi-stage plate 9A is inclined downward toward the air blowing direction, and this inclination angle ( ⁇ ) is 15 to 40 degrees with respect to the horizontal plane, preferably 15 degrees to 30 degrees.
  • This inclination angle ( ⁇ ) is set to an angle at which the incinerated material can be evenly dispersed on both sides and forward and dropped.
  • the uppermost multi-stage plate 9A has a tapered shape toward the blowing direction by gradually narrowing the lateral width of the uppermost inclined plate 10A provided on both sides.
  • the lateral width of the tip is abruptly narrowed in the blowing direction.
  • the uppermost inclined plate 10A of this shape incinerates the incinerated product supplied on the upper side while sliding it down on both sides and in the blowing direction, so that the incinerated product supplied on the upper surface can be diffused in the both sides and forward and efficiently incinerated.
  • the uppermost inclined plate 10A can be disposed in a horizontal posture without inclining the top edge 16 in a downward slope, and the incinerated material can be incinerated by sliding it down only on both sides.
  • the lower multi-stage plate 9B has a lower inclined plate 10B that protrudes outward from the uppermost inclined plate 10A and is inclined downward toward the outer side.
  • the lower multi-stage plate 9B is arranged in a plurality of stages, and a ventilation gap 11 is provided between the lower multi-stage plates 9B.
  • the lower inclined plate 10 ⁇ / b> B has a shape in which a part of the inner side is wrapped inside the upper inclined plate 10 and both side portions are projected to the outside of the upper inclined plate 10.
  • the lower inclined plate 10B shown in the drawing is formed by connecting two metal plates in a V-shape, inside the rooster 7, that is, below the uppermost inclined plate 10A and inside the lower inclined plate 10B. A gap is provided.
  • the rooster 7 has a feature that air can be smoothly blown from the air gap 11 between the inclined plates that are forcedly blown into the gap and arranged in multiple stages.
  • the lower multi-stage plate 9B provided in multiple stages has a posture in which the air gap 11 is narrowed toward the air blowing direction and inclined downward toward the air blowing direction. The angle at which the lower multi-stage plate 9B is inclined downwardly toward the blowing direction is gradually reduced toward the lower stage.
  • the lower multi-stage plate 9 ⁇ / b> B, the lowermost inclined plate 10 ⁇ / b> B, is provided with a blowing gap 11 that is substantially equal in the blowing direction between the partition plate 4.
  • the lower multi-stage plate 9B arranged in three stages has a tapered shape, and has a shape in which the tip edge is cut in a direction perpendicular to the blowing direction.
  • the lower multi-stage plate 9B arranged at the lowermost stage protrudes at the most distal end of the rooster 7. Therefore, the lower edge of the lower plate 9B is arranged in parallel with the wall of the primary combustion chamber 1 as a shape in which the leading edge is cut in a direction perpendicular to the blowing direction. Yes.
  • the incinerator of FIG. 1 arranges the primary combustion chamber 1 on the secondary combustion chamber 2, and the wall surface (the wall surface on the left side in FIG. 1) provided on the end surfaces of the primary combustion chamber 1 and the secondary combustion chamber 2 is vertical.
  • the primary combustion chamber 1 is disposed on the secondary combustion chamber 2.
  • the secondary combustion chamber 2 has a shape elongated in the flow direction of the combustion gas, is longer than the primary combustion chamber 1, and a heat exchanger 18 is disposed on the discharge side.
  • a chimney 19 is connected to the discharge side of the secondary combustion chamber 2.
  • the primary combustion chamber 1 is provided with a blower opening on a wall 20 facing the vertical wall 17 and a blower 8 is connected to the blower opening.
  • the blower 8 injects outside air into the primary combustion chamber 1 in the horizontal direction and forcibly blows air into the rooster 7.
  • the forcedly blown air is blown toward the back of the rooster 7 and blown into the rooster 7.
  • the rooster 7 is arranged with the back side facing the facing wall 20 so that the air flowing in from the back side is blown out from the ventilation gap 11.
  • the rooster 7 is disposed at a position where the back surface approaches the opposing wall 20 or contacts the opposing wall 20.
  • the primary combustion chamber 1 is incinerated to be supplied to the primary combustion chamber 1 with a length (L) in the air blowing direction of, for example, 1 to 2 times, preferably 1.1 to 1.5 times the total length of the rooster 7. Can be efficiently incinerated on the rooster 7.
  • the blower 8 is connected to an inverter 12 that adjusts the rotational speed of the motor that rotates the fan in order to control the air volume and the speed of the air supplied to the rooster 7.
  • the inverter 12 controls the rotational speed of the motor by adjusting the power supplied to the motor.
  • the inverter 12 adjusts the supply power of the motor by adjusting the voltage and frequency supplied to the motor. If the voltage and frequency supplied to the motor by the inverter 12 are lowered and the supplied power is lowered, the rotational speed of the motor is reduced.
  • the inverter 12 restricts the rotational speed of the motor to be lower than a predetermined rotational speed that rotates at the rated voltage and the rated frequency, thereby reducing the flow rate of the air forcedly blown to the rooster 7 and adjusting the flow rate to be small. This is because if the air is injected at high speed from the blower gap 11 of the rooster 7, the incinerated product cannot be incinerated while being heated to a high temperature. In particular, it is important for the blower 8 to adjust the flow rate of the forcedly blown air slowly so that the air is uniformly ejected from the blow gap 11. In order to realize this state, the inverter 12 reduces the rotational speed of the fan to limit the flow velocity and the flow velocity of the air that is blown from the blower to the rooster.
  • the flow rate of forced air can be achieved by downsizing the blower.
  • the flow rate of air forcedly blown from the blower 8 is specified by the number of rotations of the fan, and the number of rotations of the fan is specified by the AC frequency supplied to the motor, so that the number of rotations of the fan does not change.
  • the blower 8 Even if the blower 8 is used, the flow velocity of the forcedly blown air hardly decreases. Therefore, the blower 8 cannot be reduced in size, and the flow rate of the air ejected from the blowing gap 11 of the rooster 7 cannot be set to an optimum value.
  • the blower 8 that adjusts the rotation speed of the motor that is, the rotation speed of the fan by the inverter 12 can be adjusted to the optimum value by changing the flow velocity and flow rate of the forced air, so that the incinerated product supplied to the rooster 7 is ideal. Can be incinerated under normal conditions
  • the inverter 12 that adjusts both the frequency and voltage of the alternating current supplied to the motor can greatly adjust the flow rate and flow rate of the air to be blown, so that while looking at the state where the incinerated product is incinerated from the inspection window 27, Or there exists the characteristic which can adjust the flow velocity and flow volume of the air supplied to the rooster 7 to an optimal value, detecting a combustion temperature with a temperature sensor.
  • the incinerator that completely burns the incinerated products in the primary combustion chamber 1 and the secondary combustion chamber 2 performs secondary combustion of the combustion gas discharged from the primary combustion chamber 1 in the secondary combustion chamber 2 and exhausts it to the outside.
  • the incinerator burns in the secondary combustion chamber without completely burning the incinerated product in the primary combustion chamber 1 and exhausts it after complete combustion.
  • the primary combustion chamber 1 limits the supply amount of air, limits the decrease in the combustion temperature due to the inflowing air, adjusts the combustion temperature high, incinerates the incinerated product at a high temperature, and partially burns the unburned gas Is supplied to the secondary combustion chamber 2 and the unburned gas is incinerated in the secondary combustion chamber 2 and exhausted to the outside.
  • the incinerator of the present invention sets the combustion temperature of the primary combustion chamber 1 to 1300 ° C. or higher, supplies a part of the incinerated product as unburned gas to the secondary combustion chamber 2, and performs secondary combustion in the secondary combustion chamber 2. It can be exhausted from the chimney as a clear gas.
  • the secondary combustion chamber 2 is provided with a blower port for secondary combustion of the unburned gas gasified in the primary combustion chamber 1, and a second blower 28 is connected thereto.
  • the primary combustion chamber 1 is provided with a gas flow path 6 of combustion gas on the vertical wall 17 side, and combustion gas containing unburned gas flows into the secondary combustion chamber 2 from the primary combustion chamber 1.
  • the secondary combustion is performed while the combustion gas flowing into the end flows to the other end, and then passes through the discharge side provided with the heat exchanger 18 and is discharged from the chimney to the outside.
  • the vertical wall 17 opens inspection windows 21 in both the primary combustion chamber 1 and the secondary combustion chamber 2.
  • the inspection window 21 is closed by a heat-resistant glass (not shown) that can be opened and closed so that air flow can be blocked.
  • the inspection window 21 of the primary combustion chamber 1 observes the incineration state of the incinerated material supplied to the rooster 7.
  • the inspection window 21 of the secondary combustion chamber 2 inspects the internal combustion state and inserts a temperature sensor from here to detect the combustion temperature of the secondary combustion chamber 2.
  • an ignition burner 22 is connected in the vicinity of the inspection window 21.
  • the burner injects flame in a state where the incinerated product is supplied to the primary combustion chamber 1, and ignites the incinerated product supplied on the rooster 7. After igniting the incinerator, the burner stops operation and stops the flame injection. This is because the incinerated product supplied one after another is heated by the thermal energy that the incinerated product burns, and this is vaporized and incinerated at a high temperature.
  • An incinerator that uses bamboo chips that are crushed bamboo as an incinerator can stop the burner after ignition and incinerate the bamboo chips at an extremely high temperature.
  • the incinerator prototyped by the present inventor succeeded in incinerating bamboo chips of incineration at an extremely high temperature of 1310 ° C. with the burner stopped.
  • the incineration temperature was detected by inserting a temperature sensor inside the inspection window 21 of the secondary combustion chamber 2 in FIG.
  • the burner is connected to the secondary combustion chamber, but the ignition burner is provided in the primary combustion chamber and ignites by injecting flame toward the incinerated product supplied to the rooster. You can also.
  • a second blower 28 is connected to the blower opening provided in the secondary combustion chamber 2.
  • the second blower 28 supplies air to the secondary combustion chamber 2, and unburned gas obtained by gasifying a part of the incinerated material contained in the combustion gas flowing from the primary combustion chamber 1 into the secondary combustion chamber 2. Secondary combustion of gas.
  • the second blower 28 is also adjusted in the amount of air supplied via an inverter (not shown) connected to the motor. This inverter observes the combustion state of the secondary combustion chamber 2 from the inspection window 21 or detects the combustion temperature, and further the second blower 28 so that the exhaust gas discharged from the chimney is in a clear state. Adjust the air supply amount.
  • the above incinerator operates by the following processes and incinerates various incinerators.
  • the conveyor supplies the incinerated material from the supply port 3 to the primary combustion chamber 1 through the feeder 5.
  • the feeder 5 blocks the inflow and outflow of air from the supply port 3 and drops the incinerated material onto the rooster 7. After supplying a predetermined amount of incinerated material, the feeder 5 stops supplying the incinerated material.
  • the burner is ignited and a flame is injected into the secondary combustion chamber 2. The injected flame heats the interior of the secondary combustion chamber 2 and the primary combustion chamber 1, and a part of the flame flows into the primary combustion chamber 1 from the gas flow path 6 and ignites the incinerated material in the primary combustion chamber 1.
  • the blower 8 restricts the supply amount of air supplied to the primary combustion chamber 1 to be small, or stops the supply of air and controls the incinerated product to be ignited in an ideal state.
  • the amount of air supplied from the blower 8 to the primary combustion chamber 1 is adjusted by observing the inspection window 21 of the primary combustion chamber 1 and controlling the rotational speed of the motor of the blower 8 with the inverter 12. 3.
  • the amount of air supplied to the primary combustion chamber 1 by the blower 8 is controlled.
  • the amount of air supplied is adjusted by the inverter 12 by looking at the combustion state of the incinerated product placed on the rooster 7 from the inspection window 21 and adjusted until the incinerated product is stably incinerated.
  • the operation of the second blower 28 is started, and the amount of air supplied to the secondary combustion chamber 2 is adjusted by the inverter 12.
  • the amount of air supplied to the second blower 28 is such that the combustion state of the secondary combustion chamber 2 is observed from the inspection window 21 or the combustion temperature is detected by a temperature sensor, and the exhaust gas discharged from the chimney is clear.
  • the rotational speed of the motor is controlled and adjusted via the inverter 12 so as to be in a state. 4).
  • the incinerated product is stably incinerated at a constant combustion temperature
  • the combustion temperature of the incinerated product is stabilized at a constant temperature.
  • the feeder 5 removes a certain amount of the incinerated product into the primary combustion chamber. 1 is set to be supplied.
  • the amount of air supplied from the blower 8 and the second blower 28 is the rotation of the motor by the inverter 12 so that the primary combustion chamber 1 and the secondary combustion chamber 2 are burned in an ideal state.
  • the number is adjusted and set to the optimum value.
  • the inverter 12 maintains the motor rotation speed at a set value, and the feeder 5 supplies the incinerated product in a fixed quantity and continuously incinerate the incinerated product. To do.
  • the incinerator of the present invention can be conveniently used for incineration of incinerated materials at a high temperature.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Incineration Of Waste (AREA)

Abstract

Le problème à résoudre par la présente invention est d'incinérer un article à incinérer à une température élevée avec une structure simple de façon à générer un gaz d'échappement clair avec moins de cendres d'incinération et de substances nocives générées. La solution selon l'invention porte sur un incinérateur qui est configuré de telle sorte qu'une chambre de combustion secondaire 2 est disposée au-dessous d'une chambre de combustion primaire 1 dans laquelle une grille 7 est disposée, un gaz de combustion s'écoule de la chambre de combustion primaire 1 dans la chambre de combustion secondaire 2 située au-dessous, la chambre de combustion primaire 1 coupe l'air, l'article à incinérer est amené sur la grille 7, la grille 7 est pourvue d'une pluralité de plaques à plusieurs étages 9 stratifiées en plusieurs étages par l'intermédiaire d'un espace de soufflage d'air 11, les plaques à plusieurs étages 9 sont des plaques inclinées à plusieurs étages 10 qui s'inclinent vers le bas vers l'extérieur sur les deux côtés d'un bord supérieur 16, une plaque inclinée d'étage inférieur 10B fait saillie d'un étage supérieur vers l'extérieur, et une soufflante 8 qui souffle de l'air de force dans la grille 7, et souffle de l'air à travers l'espace de soufflage d'air 11 vers l'extérieur, ce qui permet d'incinérer l'article à incinérer.
PCT/JP2017/047167 2016-12-28 2017-12-28 Incinérateur Ceased WO2018124261A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2016-255876 2016-12-28
JP2016255876A JP6324482B1 (ja) 2016-12-28 2016-12-28 焼却炉

Publications (1)

Publication Number Publication Date
WO2018124261A1 true WO2018124261A1 (fr) 2018-07-05

Family

ID=62143808

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2017/047167 Ceased WO2018124261A1 (fr) 2016-12-28 2017-12-28 Incinérateur

Country Status (2)

Country Link
JP (1) JP6324482B1 (fr)
WO (1) WO2018124261A1 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109099428B (zh) * 2018-08-23 2019-11-26 东阳市天齐知识产权运营有限公司 一种垃圾处理焚烧炉

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49106152A (fr) * 1973-02-15 1974-10-08
JPS60138307A (ja) * 1983-12-24 1985-07-23 Sanenerugii Kk 固形燃料の燃焼装置
JPH066924U (ja) * 1992-06-16 1994-01-28 敏之 大蔵 焼却炉
JP2008215719A (ja) * 2007-03-05 2008-09-18 Takeo Hirahara 下方ガス化燃焼構造に混合燃焼室を設けたボイラー
US20100242941A1 (en) * 2009-03-26 2010-09-30 Palmer Bradley C Grate assembly

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49106152A (fr) * 1973-02-15 1974-10-08
JPS60138307A (ja) * 1983-12-24 1985-07-23 Sanenerugii Kk 固形燃料の燃焼装置
JPH066924U (ja) * 1992-06-16 1994-01-28 敏之 大蔵 焼却炉
JP2008215719A (ja) * 2007-03-05 2008-09-18 Takeo Hirahara 下方ガス化燃焼構造に混合燃焼室を設けたボイラー
US20100242941A1 (en) * 2009-03-26 2010-09-30 Palmer Bradley C Grate assembly

Also Published As

Publication number Publication date
JP6324482B1 (ja) 2018-05-16
JP2018105604A (ja) 2018-07-05

Similar Documents

Publication Publication Date Title
CN100467948C (zh) 炉篦式废弃物焚烧炉及其燃烧控制方法
TW202117254A (zh) 多燃燒器旋轉爐熔化系統及方法
KR101063516B1 (ko) 경사푸셔식 폐기물 및 폐자원 고형연료 전용 연소 보일러 장치
JP6324482B1 (ja) 焼却炉
CN87105538A (zh)
JP2010271002A (ja) 陶芸用薪窯
JP6218117B2 (ja) 火格子式廃棄物焼却炉及び廃棄物焼却方法
EP2906873B1 (fr) Procédé et dispositif d'intensification du brûlage de combustibles solides dans un foyer
WO2014015550A1 (fr) Poêle à biocombustible anti-retour de flammes
KR100977012B1 (ko) 기압차를 이용한 연소장치 겸용 보일러
JP6256859B2 (ja) 廃棄物焼却方法
JP3754683B2 (ja) 竪型ごみ焼却炉及びこの竪型ごみ焼却炉における高発熱量廃棄物の燃焼制御方法
PT2775201E (pt) Método operacional para um aquecedor
JP5490956B1 (ja) 焼却装置
JP2010133697A (ja) 粒状燃料の燃焼器
JP6270980B1 (ja) 焼却炉
JP2018059642A (ja) 燃焼装置およびこれを用いた熱供給システム
ES1126705U (es) Parrilla de quemado para quemadores de biomasa y quemador de biomasa.
JP2004163009A (ja) 廃棄物焼却システムの操業方法及び廃棄物焼却システム
JP2015081701A (ja) 燃焼炉及び燃焼炉で流動性固体燃料を燃焼させる方法
JP3075702U (ja) 焼却炉
JP4068483B2 (ja) 溶融炉
JP3099588U (ja) 小型の固定床型焼却炉
KR101457301B1 (ko) 펠릿연료 예비연소장치
JP2005155982A (ja) 燃焼炉

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 17888294

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 17888294

Country of ref document: EP

Kind code of ref document: A1