JP6333021B2 - Incineration processing equipment and incineration processing method - Google Patents

Description

  The present invention relates to an incineration processing facility and an incineration processing method.

  Patent Document 1 aims to provide a waste incineration facility and a processing method that are excellent in energy efficiency without requiring a blower for generating compressed air for combustion and compressed air for preventing white smoke and supplying it to a preheater. And a first preheater for preheating combustion compressed air supplied to the fluidized bed incinerator by continuous gas-gas heat exchange with the exhaust gas from the fluidized bed incinerator. The turbine is rotated by compressed air for combustion which is heated by the first preheater and goes to the fluidized bed incinerator, and the compressor generates and blows compressed air to be supplied to the first preheater by this rotation. A waste treatment facility including a turbine device serving as a supercharger and a first start-up air supply device that is provided upstream of the first preheater and rotates the turbine at the start of operation has been proposed.

Japanese Patent No. 4831309

  When incinerating biomass such as sewage sludge in the waste treatment facility disclosed in Patent Document 1, the in-furnace combustion temperature is set to suppress the generation amount of nitrous oxide that causes global warming. It is necessary to incinerate at a high temperature of 850 ° C. or higher. For this reason, when sludge having a high water content is incinerated, fossil fuel is supplied to the combustion burner for auxiliary heating.

  However, when high-calorie biomass such as sewage sludge with low moisture content is incinerated, the temperature may exceed 900 ° C., and the object to be treated starts sintering, and the clinker is placed on the inner wall of the furnace and the flue. May adhere to the gas, impairing gas flow, and may cause clogging.

  Therefore, if a water spray device is installed in the furnace to avoid an abnormal temperature rise in the furnace, the total amount of exhaust gas increases due to the generated steam, leading to an increase in the size of the exhaust gas treatment facility at the latter stage, and the economic efficiency of the facility is impaired. was there.

  Moreover, in order to maintain a negative pressure inside the furnace, it is necessary to provide an induction blower that consumes a large amount of power in the flue, and there is room for further improvement in terms of improving energy efficiency.

  Furthermore, when exhaust gas is pumped to the flue with the residual pressure of the compressed air for combustion without installing an induction blower, high-temperature exhaust gas is discharged from each exhaust gas treatment facility disposed in the furnace chamber or flue that is at positive pressure. There is a problem that it is necessary to securely seal so as not to be blown out, which causes an increase in equipment cost, and there is a problem that if the seal is broken, high-temperature exhaust gas is blown out, leading to a serious accident.

  In view of the above-mentioned problems, the object of the present invention is to adjust the combustion temperature without increasing the size of the equipment and to consume a large amount of power while using the compressed air from the turbine device as combustion air. It is the point which provides the incineration processing equipment and the incineration processing method which can maintain the inside of a furnace to a negative pressure, without providing an induction blower.

In order to achieve the above object, the first characteristic configuration of the incineration processing system according to the present invention is an incinerator to which high-temperature compressed air is supplied as combustion air, as described in claim 1 of the claims, a first heat exchanger for preheating the compressed air by heat retained in the exhaust gas is guided to the flue of the incinerator, and a turbine rotated by compressed air high temperature preheated by the first heat exchanger, the rotation of the turbine A turbine device including a compressor for supplying compressed air to the first heat exchanger, and a combustion air supply path for supplying high-temperature compressed air after driving the turbine to the incinerator as combustion air; a incineration facility comprises a, is disposed in the incinerator, and抽熱unit for further preheating the preheated hot compressed air in the furnace combustion heat in the first heat exchanger, generated by the compressor Is via a mixing ratio adjusting mechanism for adjusting the mixing ratio of the compressed air generated by said first said compressor and compressed air preheated in the heat exchanger without going through the first heat exchanger, the抽熱unit By adjusting the amount of heat exchange, a temperature adjusting mechanism for adjusting the in-furnace combustion temperature of the incinerator is provided.

Compressed air generated by the compressor is further sent to the extractor via the first heat exchanger, where heat is exchanged with the combustion heat in the furnace. As a result, an abnormal rise in the furnace temperature is suppressed. The The temperature adjustment mechanism adjusts the amount of compressed air supplied to the extractor, for example, to keep the furnace temperature in the range of 850 ° C. to 900 ° C., thereby reducing the amount of nitrous oxide generated while reducing the amount of exhaust gas. an increase in the amount ing to be able to avoid clinker adhering to no furnace wall or flue can lead.

Then, the mixed-rate control mechanism, by increasing the mixing ratio of the compressed air before than compressed air preheated in the first heat exchanger is preheated by the first heat exchanger, heat at much抽熱unit The amount of exchange can be increased and the furnace combustion temperature can be effectively reduced.

In the second characteristic configuration, as described in the second aspect, in addition to the first characteristic configuration described above, the temperature adjustment mechanism includes the compressed air preheated by the first heat exchanger and the first characteristic configuration . Compressed air that does not pass through the heat exchanger is configured by a mixing ratio adjusting mechanism that adjusts the mixing ratio while supplying the total amount of compressed air supplied into the furnace and supplies it to the extractor.

  If the mixing ratio of the compressed air before being preheated in the first heat exchanger is made larger than the compressed air preheated in the first heat exchanger by the mixing ratio adjusting mechanism, the heat exchange amount in the extractor is correspondingly increased. In addition, the combustion temperature in the furnace can be effectively reduced, and the total amount of compressed air supplied into the furnace is adjusted to be constant, so that the combustion state formed by the compressed air supplied into the furnace can be reduced. It can be stabilized.

The third feature structure, as described in the claim 3, in addition to the first or second characteristic feature of the above, obtained by collecting the furnace heat of combustion and / or exhaust gas potential heat movement An exhaust gas attracting device for attracting the exhaust gas guided to the flue using energy is provided.

  The turbine is driven by the high-temperature compressed air from which the retained heat or combustion heat of the exhaust gas is recovered by the first heat exchanger and / or the extractor, and the compressor connected to the turbine is driven to generate compressed air. Since the exhaust gas induction device attracts the exhaust gas guided to the flue by using the kinetic energy generated from the retained heat or combustion heat of the exhaust gas recovered at this time, the exhaust gas induction device such as the electric power for driving the induction fan Separate energy is not required, energy efficiency can be further improved, and the inside of the furnace can be maintained at a negative pressure.

In the fourth feature configuration, as described in claim 4 , in addition to the third feature configuration described above, the exhaust gas attraction device discharges the exhaust gas guided to the flue from the turbine. It is in the point comprised by the ejector attracted by the flow of hot compressed air.

  Part of the high-temperature compressed air that is discharged from the turbine and supplied to the incinerator as combustion air is supplied to the air supply port of the ejector, and flue gas is drawn from the vacuum port and flows out to the diffuser. The interior of the furnace is maintained at a negative pressure without an induction blower driven by electric power. In addition, since the exhaust gas is heated by being mixed with high-temperature compressed air by the diffuser, the anti-whitening effect is also realized by raising the temperature and reducing the humidity of the exhaust gas.

In the fifth feature configuration, as described in claim 5 , in addition to the third feature configuration described above, the exhaust gas attraction device includes an induction fan whose rotational shaft is driven by the shaft power of the turbine device. It is in the point where it is prepared.

  The induction blower is rotationally driven by the shaft power of the turbine driven by the high-temperature compressed air that collects the retained heat of the exhaust gas by the first heat exchanger, and the flue exhaust gas is attracted. That is, no separate electric power is required to rotationally drive the induction fan.

In the sixth feature configuration, in addition to any of the first to fifth feature configurations described above, the compressed air generated by the compressor is discharged from the turbine, as described in claim 6 . A second heat exchanger preheated with high-temperature compressed air is provided, and the compressed air preheated by the second heat exchanger is configured to be supplied to the first heat exchanger.

  By providing the second heat exchanger, the amount of heat brought in by the compressed air supplied to the turbine can be increased, and the amount of compressed air generated by the compressor can be increased. For example, when a generator is connected to the turbine, the amount of power generation can be further increased. Since the second heat exchanger is air for both the preheating source and the preheating target, unlike the exhaust gas containing acidic components, it does not cause low-temperature corrosion, so that the amount of heat of the preheating source can be recovered with high efficiency.

In addition to any one of the first to sixth feature configurations described above, the seventh feature configuration is biomass having a high calorie content to be treated in the incinerator. In that point.

  It is preferable that the material to be incinerated in the incinerator is high-calorie biomass including, for example, woody, and it is possible to incinerate at a sufficiently high temperature with high energy efficiency, so sub-oxidation that is a cause gas of global warming The amount of nitrogen generated can also be suppressed extremely effectively.

The first characteristic configuration of the incineration treatment method according to the present invention is that, as described in claim 8 , compressed air is generated by a compressor that operates in conjunction with a turbine, and the compressed air is generated by the retained heat of the exhaust gas guided to the flue of the incinerator. Is an incineration processing method in which the turbine is rotated by preheated high-temperature compressed air, and the high-temperature compressed air after driving the turbine is supplied to the incinerator as combustion air, which is generated by the compressor. Compressed air before being supplied to the turbine, which is compressed air in which the mixing ratio of compressed air preheated by the retained heat of the exhaust gas and compressed air generated by the compressor and not preheated by the retained heat of the exhaust gas is adjusted by preheating the furnace heat of combustion of the incinerator, and lies in adjusting the furnace combustion temperature of the incinerator.

  As described above, according to the present invention, an induction blower that can adjust the combustion temperature without increasing the size of the facility and consumes large electric power while using the compressed air from the turbine device as combustion air. It is now possible to provide an incineration treatment facility and an incineration treatment method capable of maintaining the inside of the furnace at a negative pressure without providing a gas.

Explanatory drawing of incineration processing equipment and incineration processing method by the present invention Explanatory drawing of incineration processing equipment showing another embodiment Explanatory drawing of incineration processing equipment showing another embodiment

Hereinafter, embodiments of the incineration processing equipment and the incineration processing method according to the present invention will be described.
FIG. 1 shows an incineration processing facility 1. The incineration processing facility 1 includes a silo 10 in which biomass is stored, a biomass charging mechanism 11, and a fluidized bed incinerator 2 to which high-temperature compressed air is supplied as flowing air. Along the flue of the fluidized bed incinerator 2, the first heat exchanger 20, a highly heat-resistant dust collector 16 equipped with a ceramic filter, and an alkali agent are sprayed to neutralize acid gas components in the exhaust gas. A flue gas processing tower 17 and a chimney 18 are disposed. Reference numeral 12 denotes a combustion burner.

  Biomass, which is an object to be treated by the incineration facility 1, is generated in a sewage treatment facility that employs a method such as an activated sludge method that biologically treats sewage sludge or a membrane separation activated sludge method that performs biological treatment and membrane filtration High-calorie biomass derived from various animals and plants is included, such as dry sludge from which excess sludge has been sufficiently dehydrated and high-calorie organic sludge such as sludge generated by purifying sewage generated at food factories.

  The incineration treatment facility 1 includes a turbine 31 that is rotated by high-temperature compressed air preheated by the first heat exchanger 20 and a compressor 32 that supplies compressed air to the first heat exchanger 20 by the rotation of the turbine 31. A turbine device 30 is provided.

  A compressor 32 connected to the turbine 31 is driven to generate compressed air of 100 to 150 ° C. and 0.2 to 0.3 MPa, and the compressed air generated by the compressor 32 is supplied to the first heat exchanger 20. Thus, it is preheated to 650 to 750 ° C. and 0.2 to 0.3 MPa by the retained heat of the exhaust gas at about 900 ° C. guided to the flue of the fluidized bed incinerator 2. In addition, the pressure demonstrated in this specification is a gauge pressure.

  When the compressed air preheated by the first heat exchanger 20 is supplied to the turbine 31, the turbine 31 is rotationally driven, and the compressor 32 connected to the drive shaft is driven. A part of the compressed air of 500 to 600 ° C. and 0.05 to 0.15 MPa discharged from the turbine 31 is supplied to the fluidized bed incinerator 2 as fluidizing air, that is, combustion air, to form a fluidized bed. Further, a generator G is connected to the output shaft of the turbine device 30 so that power can be generated by the rotational power of the turbine 31.

  The high-calorie biomass input into the furnace by the biomass input mechanism 11 is heated and pyrolyzed in the fluidized bed without igniting the combustion burner 12, and the pyrolysis gas burns at about 850 ° C to 900 ° C. Since it flows out into the flue, generation of nitrous oxide, which is a global warming gas, during combustion of sludge is suppressed.

  Further, the incineration treatment facility 1 includes an exhaust gas attracting device 40 that attracts the exhaust gas guided to the flue using the kinetic energy obtained by collecting the retained heat of the exhaust gas by the turbine device 30.

  A part of the compressed air of 500 to 600 ° C. and 0.05 to 0.15 MPa discharged from the turbine 31 is supplied to the exhaust gas induction device 40. The exhaust gas attracting device 40 attracts exhaust gas guided to the flue by using kinetic energy generated from the retained heat of the exhaust gas recovered by the first heat exchanger 20 and discharges it from the chimney 18.

  The exhaust gas attracting device 40 is composed of an ejector that attracts the exhaust gas guided to the flue by the flow of high-temperature compressed air discharged from the turbine 31.

  A part of the high-temperature compressed air discharged from the turbine 31 and supplied as fluidized air to the fluidized bed incinerator 2 is supplied to the air supply port 40a constituting the ejector, and the flue gas is sucked from the vacuum port 40b. As a result, it flows out into the diffuser 40c, so that the inside of the furnace is maintained at a negative pressure without an induction blower driven by electric power. Moreover, since the exhaust gas that has been reduced to about 40 ° C. in the flue gas treatment tower 17 is mixed with high-temperature compressed air and heated in the diffuser 40c, the white prevention effect is also realized due to the temperature rise and humidity reduction of the exhaust gas. It becomes like this. A part of the high-temperature compressed air may be supplied to the chimney 18 side without going through the ejector for white protection.

  In order to control the combustion state of the fluidized bed incinerator 2, when it is necessary to adjust the input amount or temperature of the flowing air, the air supply amount to the compressor 32 may be configured by the flow rate adjusting valve V1. Further, a valve V4 that adjusts the supply amount of the compressed air output from the turbine 31 to the fluidized bed incinerator 2 and the supply amount to the exhaust gas induction device 40 may be provided in the compressed air conveyance path. Hereinafter, an example in which a valve is used as a mechanical element for adjusting the flow rate will be described. However, a damper may be used as a mechanical element for adjusting the flow rate.

  According to such a configuration, no separate energy such as electric power for driving the conventional induction fan is required, energy efficiency can be further improved, and the inside of the furnace can be maintained at a negative pressure. Further, it is not necessary to provide a special sealing mechanism that requires equipment costs.

  The incineration treatment facility 1 includes an extractor 50 that further preheats high-temperature compressed air preheated by the first heat exchanger 20 with in-furnace combustion heat, and the combustion temperature of the fluidized bed incinerator 2 is within a target temperature range. The temperature adjustment mechanism 70 which adjusts the heat exchange amount of the extractor 50 so that it may enter is provided.

  The temperature adjusting mechanism 70 branches in the middle of the preheating path L1 for supplying the compressed air generated by the compressor 32 to the first heat exchanger 20, and the compressed air preheated by the first heat exchanger 20 is extracted by the extractor 50. Control for adjusting the opening degree of the valves V2 and V3, the branch path L2 that joins the path leading to the flow path, the flow rate adjusting valve V2 provided in the branch path L2, the flow rate adjusting valve V3 provided in the preheating path L1 Part 71.

  The temperature adjustment mechanism 70 controls the opening degree of the valves V2 and V3 so that the furnace temperature measured by the temperature sensor TS is maintained within a predetermined temperature range, and the amount of compressed air supplied to the extractor 50 and / Or adjust the temperature. Specifically, when the combustion temperature in the furnace rises above 900 ° C., the supply amount of compressed air is increased and / or the temperature is decreased to increase the extraction heat amount. When the combustion temperature falls below 850 ° C., the supply amount of compressed air is decreased. And / or increase the temperature to reduce the amount of extracted heat.

  For example, PID calculation is performed to adjust the amount of extracted heat based on a difference value, a differential value, an integral value, etc. between the target temperature and the furnace temperature so that the furnace temperature measured by the temperature sensor TS falls within the target temperature range. Thus, the opening degree of the valves V2 and V3 is controlled, and as a result, the furnace temperature is maintained in the range of 850 ° C to 900 ° C. This makes it possible to avoid the clinker from adhering to the furnace wall and the flue without increasing the amount of exhaust gas while reducing the amount of nitrous oxide generated. Note that only the valve V2 may be provided and the valve V3 may not be provided.

  A mixing ratio for adjusting the mixing ratio of the compressed air preheated by the first heat exchanger 20 and the compressed air before being preheated by the first heat exchanger 20 to the temperature adjusting mechanism 70 to be supplied to the extractor 50 It is preferable that the adjustment mechanism is used, and if the mixing ratio of the compressed air before being preheated by the first heat exchanger 20 is made larger than the compressed air preheated by the first heat exchanger 20, the amount of the extractor 50 is increased accordingly. The amount of heat exchange in the furnace can be increased, and the combustion temperature in the furnace can be effectively reduced.

  Further, the temperature adjusting mechanism 70 is configured so that the compressed air preheated by the first heat exchanger 20 and the compressed air before preheated by the first heat exchanger 20 are made constant in the total amount of compressed air supplied into the furnace. However, it is more preferable that the mixing ratio is adjusted and the mixing ratio is adjusted to be supplied to the extractor 50, and compressed before being preheated by the heat exchanger rather than the compressed air preheated by the first heat exchanger 20. If the air mixing ratio is increased, the amount of heat exchange in the extractor 50 can be increased accordingly, and the furnace combustion temperature can be effectively reduced, and the total amount of compressed air supplied into the furnace can be kept constant. Since it is adjusted, the state of the fluidized bed formed by the compressed air supplied into the furnace can be stabilized.

  At this time, surplus compressed air is preferably supplied to the exhaust gas induction device 40 or supplied for white smoke prevention, and may be used exclusively for energy generation.

  In addition, a water spray mechanism is provided on the furnace ceiling of the fluidized bed incinerator 2 or a water pipe is provided on the furnace wall in case the abnormal rise in combustion temperature in the furnace cannot be suppressed only by adjusting the supply amount of compressed air. And a temperature adjustment assisting mechanism for adjusting the furnace temperature by adjusting the amount of cooling water supplied to the water pipe or water spray. In this case, the temperature adjustment mechanism 70 is configured to adjust the supply amount of compressed air in preference to the temperature adjustment auxiliary mechanism, and the temperature adjustment auxiliary mechanism is used when the adjustment cannot be made to the target temperature range only by the supply amount of compressed air. It is preferably configured to control.

  When the fluidized bed incinerator 2 is started up, the generator G is operated as a motor, the turbine is rotated by a motor driven by external power, the combustion burner 12 is ignited, and the object to be processed is charged when the furnace is warmed Then, the incineration process is started, the generator G operated as a motor is stopped, and then operated as a generator. In addition, when the generator G is not provided, it is also possible to start by supplying fossil fuel to the combustor provided in the turbine 31.

  The numerical values such as pressure and temperature shown in the above-described embodiments are merely examples, and the present invention is not limited to the numerical values. In addition, the exhaust gas induction device 40 and other parts of the incineration treatment facility 1 are included. The specific configuration such as the structure, size, material, and the like can be changed and designed as appropriate within the range in which the effects of the present invention can be achieved. The same applies to the following description.

  As shown in FIG. 2, the compressed air generated by the compressor 32 is provided with a second heat exchanger 24 for preheating with high-temperature compressed air discharged from the turbine 31, and the compression preheated by the second heat exchanger 24 is provided. It is preferable that air is supplied to the first heat exchanger 20.

  By providing the second heat exchanger 24, the amount of heat brought in by the compressed air supplied to the turbine 31 can be increased, and the amount of compressed air generated by the compressor 32 can be increased. For example, when the generator G is connected to the turbine 31, the power generation amount can be further increased.

  At this time, the compressed air before heat exchange in the second heat exchanger 24 is supplied to the exhaust gas attraction device 40, and the compressed air heat-exchanged in the second heat exchanger 24 is directed to the chimney 18 side as air for white protection. It is preferable to be configured to be supplied.

  In addition, since the third heat exchanger 24 is air for both the preheating source and the preheating target, unlike the exhaust gas containing acidic components such as sulfur, it does not cause low-temperature corrosion, so the heat amount of the preheating source is recovered with high efficiency. become able to.

  As shown in FIG. 3, the exhaust gas attracting device 40 can also be configured by an attracting blower F whose rotating shaft is driven by the shaft power of the turbine device 30.

  The induction blower F is rotationally driven by the shaft power of the turbine 31 driven by the high-temperature compressed air that has recovered the retained heat of the exhaust gas by the first heat exchanger 20, and the flue exhaust gas is attracted. That is, no separate electric power is required to rotationally drive the induction fan F.

  Also in this case, white smoke can be prevented without providing a separate white smoke prevention fan by guiding the high-temperature compressed air output from the turbine 31 to the flue downstream of the smoke treatment tower 17. .

  That is, the exhaust gas attraction apparatus 40 according to the present invention uses the kinetic energy obtained by recovering the retained heat of the exhaust gas by the turbine device 30, mechanical kinetic energy called rotational force, and kinetic energy called fluid flow velocity to the flue. Any structure that induces the exhaust gas that has been introduced may be used.

  As described above, the material to be incinerated in the fluidized bed incinerator 2 is preferably biomass containing sewage sludge, and can be incinerated at a sufficiently high temperature with high energy efficiency, thereby causing global warming. The generation amount of nitrous oxide, which is a gas, can be suppressed extremely effectively.

  As described above, the incineration processing method according to the present invention generates compressed air by the compressor 32 interlocked with the turbine 31 and preheats the compressed air by the retained heat of the exhaust gas guided to the flue of the fluidized bed incinerator 2. The incineration processing method of rotating the turbine 31 with preheated high-temperature compressed air and supplying the high-temperature compressed air after driving the turbine 31 to the fluidized bed incinerator 2 as flow air, This is an incineration processing method in which high-temperature compressed air before being supplied is preheated by the in-furnace combustion heat of the fluidized bed incinerator 2 and the in-furnace combustion temperature of the fluidized bed incinerator 2 is adjusted.

  In addition, compressed air is generated by a compressor linked to the turbine, and the compressed air is preheated by the in-furnace combustion heat of the incinerator and / or the retained heat of the exhaust gas introduced into the flue, and the turbine is heated by the preheated high-temperature compressed air. It is an incineration treatment method in which high-temperature compressed air that is rotated and exhausted from a turbine is introduced into an incinerator through a pipe, and is introduced into a chimney through a pipe for anti-white protection or exhaust gas reference.

  As a turbine device in which a turbine and a compressor are axially connected, it is possible to adopt a configuration in which a compressor is axially connected to an expansion turbine used for not only a supercharger but also cold power generation.

  The embodiment described above has been described for the case where a fluidized bed incinerator is adopted as an incinerator, but the incinerator to which the present invention is applied is not limited to a fluidized bed incinerator, a stoker furnace, a kiln furnace, a jet flow furnace, It can also be applied to other types of incinerators such as melting furnaces.

  Each of the above-described embodiments is an example of the present invention, and the present invention is not limited by the description. The specific configuration of each part can be appropriately changed and designed within the range where the effects of the present invention are exhibited. Needless to say.

1: incineration equipment 2: fluidized bed incinerator 10: silo 20: first heat exchanger 24: second heat exchanger 30: turbine device 31: turbine 32: compressor 40: exhaust gas induction device 40a: air supply port 40b : Vacuum port 40c: Diffuser 50: Extractor 70: Temperature adjustment mechanism

Claims (8)

An incinerator supplied with high-temperature compressed air as combustion air;
A first heat exchanger that preheats compressed air with retained heat of exhaust gas guided to the flue of the incinerator;
A turbine which is rotated by compressed air high temperature preheated by the first heat exchanger, a turbine unit including a compressor for supplying compressed air to the first heat exchanger by the rotation of the turbine,
A combustion air supply path for supplying high-temperature compressed air after driving the turbine to the incinerator as combustion air;
An incineration treatment facility comprising:
An extractor that is disposed in the incinerator and further preheats high-temperature compressed air preheated by the first heat exchanger with in-furnace combustion heat;
Through a mixing ratio adjusting mechanism that adjusts a mixing ratio of compressed air generated by the compressor and preheated by the first heat exchanger and compressed air generated by the compressor and not passing through the first heat exchanger, An incineration treatment facility provided with a temperature adjustment mechanism for adjusting the in-furnace combustion temperature of the incinerator by adjusting the heat exchange amount of the extractor. The temperature adjustment mechanism adjusts the mixing ratio of the compressed air preheated in the first heat exchanger and the compressed air that does not pass through the first heat exchanger while keeping the total amount of compressed air supplied into the furnace. The incineration processing facility according to claim 1, wherein the incineration processing facility is configured by a mixing ratio adjusting mechanism that supplies the heat extracting device. The incineration process according to claim 1 or 2, further comprising an exhaust gas induction device that induces the exhaust gas led to the flue using kinetic energy obtained by recovering the combustion heat in the furnace and / or the retained heat of the exhaust gas. Facility. 4. The incineration processing equipment according to claim 3 , wherein the exhaust gas attraction device is configured by an ejector that attracts the exhaust gas guided to the flue by a flow of high-temperature compressed air discharged from the turbine. The incineration processing facility according to claim 3 , wherein the exhaust gas induction device includes an induction blower in which a rotating shaft is driven by shaft power of the turbine device. A second heat exchanger for preheating the compressed air output from the compressor with high-temperature compressed air discharged from the turbine; and supplying the compressed air preheated by the second heat exchanger to the first heat exchanger The incineration processing facility according to any one of claims 1 to 5 , wherein the incineration processing facility is configured to be supplied. The incineration processing equipment according to any one of claims 1 to 6 , wherein an object to be incinerated in the incinerator is high-calorie biomass. Compressed air is generated by a compressor that works with the turbine, and the compressed air is preheated by the retained heat of the exhaust gas that is led to the flue of the incinerator, and the turbine is rotated by the preheated high-temperature compressed air and the turbine is driven. An incineration processing method for supplying high-temperature compressed air as combustion air to the incinerator,
The compressed air generated by the compressor and preheated by the retained heat of the exhaust gas and the compressed air generated by the compressor and adjusted by the mixing ratio of the compressed air not preheated by the retained heat of the exhaust gas are supplied to the turbine. An incineration processing method for adjusting the in-furnace combustion temperature of the incinerator by preheating the compressed air before being heated with the in-furnace combustion heat of the incinerator.

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