JP2001021126A - Apparatus for dry distilating, thermal cracking, melting and igniting waste material - Google Patents

Abstract

PROBLEM TO BE SOLVED: To prevent not-yet ignited substances or odor from being dispersed by a method wherein thermal cracking gas left in a thermal cracking drum is ignited within a melting and igniting device at the time of power failure. SOLUTION: There are provided a dry distillation and thermal cracking drum 2 for changing a waste material C and thermal cracking gas G into thermal cracking sludge D; a forcing blower 26 for supplying air A for melting and ignition to a melting and igniting device 4 for melting and igniting the thermal cracking gas and thermal cracking sludge; a gas purifying device 9 for purifying ignition discharged gas G0 from a waste heat boiler 7 recovering heat of the combustion discharging gas GO0 of the melting and igniting device; a forcing blower 16; and an electrical power facility 31 for supplying an electrical power to each of the segments. The forcing blower and an induction blower are provided with steam turbines 26b, 16b applied with steam flowed from a waste boiler acting as a rotary driving device, and with electric motors 26a, 16a. A switching opening or closing device 33 is arranged at load sides of the electrical power facility 31 and an emergency power generating device 32. When an input electrical power for the electrical power facility is lost, electrical power is supplied to the forcing blower, a boiler water supplying pump, the induction blower and the rotary driving device for the thermal cracking drum.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is used for the thermal decomposition, melting and burning of waste such as municipal solid waste. Pyrolysis heat of waste, which effectively burns pyrolysis gas generated from the carbonization pyrolysis drum with the use of emergency power in the melting and burning apparatus, and eliminates any trouble caused by the discharge of unburned gas or odor to the outside. The present invention relates to a decomposition melting combustion apparatus.

[0002]

2. Description of the Related Art FIG. 2 shows an example of a conventional dry distillation pyrolysis melting and burning apparatus for waste. A waste C supplied into a dry distillation pyrolysis drum 2 by a supply device 1 is heated gas K.
Is heated to a temperature of 300 ° C. to 600 ° C. for a certain period of time under the cutoff of air, and is converted into a pyrolysis gas G and a pyrolysis residue D. Is separated into

[0003] The separated pyrolysis gas G is sent from the unloading device 3 to the melting and burning device 4 through the gas duct 25, and is burned at a high temperature by being supplied with combustion air from a forced air blower 26. Further, the pyrolysis residue D is sent to the separation device 5 and separated into a relatively coarse non-combustible solid and a fine combustible solid I. Further, the separated combustible solids I are finely pulverized by the pulverizing device 6 and then supplied to the melting and burning device 4 to be melt-combusted with the pyrolysis gas G at a temperature of 1200 ° C. or higher.

[0004] The inside of the dry distillation pyrolysis drum 2 and the melting and burning device 4 is maintained at an appropriate negative pressure by an induction ventilator 16, whereby pyrolysis gas G is sent from the dry distillation pyrolysis drum 2 to the melting and burning device 4. And the combustion exhaust gas G _O from the melting and burning device 4 is discharged to the waste heat boiler 7, the dust collector 8,
The gas is discharged into the atmosphere through a gas purification device 9 and a chimney 10. Further, the molten slag F formed in the molten combustion device 4 is sequentially taken out as granulated slag to the outside.

[0005] On the other hand, when the power supply to the waste carbonization pyrolysis melting and burning device is stopped due to a power failure or the like, generally, the operation of the induction ventilator 16 and the forced air blower 26 of the waste carbonization pyrolysis melting and burning device is not performed. Stopped. Along with this, the combustion in the melt combustion device 4 is stopped due to lack of oxygen.
On the other hand, the waste C in the pyrolysis drum 2 is continuously pyrolyzed by the residual heat even when the supply of the heating gas K is stopped, and the generated pyrolysis gas G is melted by the pressure increase in the unloading device 3. It is supplied into the combustion device 4.

In order to reduce the amount of the pyrolysis gas G generated during a power failure or the like, the number of revolutions of the pyrolysis drum 2 is greatly reduced. From this point, the thermal decomposition drum 2 is not completely stopped, and is rotated at an extremely low speed by the power of the emergency power supply.

When the pyrolysis gas G continues to be supplied from the pyrolysis drum 2 into the melting and burning device 4 in a combustion stopped state due to a power failure or the like, the pyrolysis gas G is supplied due to a shortage of combustion air due to the stoppage of the forced air blower 26. Will be emitted to the outside without being burned, which will cause environmental pollution due to odor and harmful substances.

Therefore, in the conventional dry distillation pyrolysis melting and burning apparatus, a three-way switching type switching apparatus 27 is provided in a gas duct 25 communicating between the unloading apparatus 3 and the melting and burning apparatus 4 and the switching apparatus 27 is provided with an emergency. The combustion exhaust stack 28 is connected, and in case of a power failure, the switching device 27
And the flammable pyrolysis gas G from the unloading device 3 is introduced into the emergency combustion exhaust stack 28, where the gas burner 29
Thus, the combustible pyrolysis gas G is burned.

However, as shown in FIG.
The emergency combustion exhaust stack 28 itself requires a heat-resistant structure, and it is necessary to provide a large number of gas burners 29 in order to completely burn the pyrolysis gas G. As a result, there is a problem that the size of the emergency combustion exhaust stack 28 becomes extremely large, resulting in an increase in equipment costs. Also, the emergency combustion exhaust stack 2
It is necessary to keep the gas burner 29 attached to 8 always in an ignition state in preparation for the occurrence of a power failure or the like, and there is a problem that the amount of consumed fuel increases due to the large number of gas burners 29.

As a solution to the above-mentioned drawback when the emergency combustion exhaust stack 28 is used, as shown in FIG. 3, the molten combustion air A which communicates the forced air blower 26 and the molten combustion apparatus 4 with each other. A damper device 30 is provided in the supply duct of
In the event of a power outage, the power of the emergency power supply
0 is operated to suck the auxiliary combustion air f through the damper device 30 and to supply the sucked auxiliary combustion air f into the melting and burning device 4 (Japanese Patent Laid-Open No. Hei 9 (1999)). -250727).

However, according to the technique disclosed in Japanese Patent Application Laid-Open No. 9-250727, if the operation of the push-in blower 26 and the induction ventilator 16 is stopped during a power failure, the internal pressure in the melting and burning device 4 increases in a short time. As a result, there is a problem that a necessary and sufficient amount of auxiliary combustion air f cannot be sucked into the melting and burning apparatus 4.

2 and 3, 11 is a heating tube, 12 is a hot air generator, 13 is a steam superheater, 14 is a steam turbine generator, 15 is a blower, 16 is an induction fan, 17 Is a cooling conveyor, 18 is a combustible fine powder storage tank, 1
9 is a heating gas flow path, 20 is a circulation fan, 21 is a heat exchanger, 22 is a burner, 23 is a waste pit, 24 is a waste supply crane, 25 is a gas duct, 26 is a push blower, 27 is a switchgear, 28 is an emergency combustion exhaust stack, 29 is a gas burner, 30 is a damper device, A is air for molten combustion,
f is auxiliary combustion air.

[0013]

SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems relating to the processing of "pyrolysis gas generated at the time of power failure" in a conventional dry distillation pyrolysis melting and burning apparatus for waste, that is, an emergency combustion exhaust stack. 28, the emergency combustion stack 2
8 is large, the equipment cost is increased, the amount of gas consumed by the gas burner 29 is increased, the running cost is increased, and the auxiliary combustion air f is increased via the damper device 30.
In this case, it is difficult to suck a sufficient amount of the auxiliary combustion air f, and the problem that the incomplete combustion of the pyrolysis gas G easily occurs is not solved. Yes, with a smaller-capacity emergency power facility, the pyrolysis gas G generated at the time of a power outage is completely burned in the melting and burning device 4 to economically stop environmental pollution due to emission of harmful substances and odors. It is an object of the present invention to provide an apparatus for pyrolysis melting and combustion of waste by distillation.

[0014]

According to the first aspect of the present invention, there is provided a dry distillation pyrolysis drum which pyrolyzes waste into a pyrolysis gas and a pyrolysis residue, and a combustible material in the pyrolysis gas and the pyrolysis residue. A melt-burning device that melts and burns the melt-burning device, a forced air blower that supplies melt-burning air to the melt-burning device, and a waste heat boiler that is provided downstream of the melt-burning device and recovers heat of combustion exhaust gas from the melt-burning device. A gas purification device for purifying combustion exhaust gas from a waste heat boiler, an induction ventilator provided downstream of the gas purification device, a chimney for discharging combustion exhaust gas from the induction ventilator to the atmosphere, and A waste heat boiler as a rotary drive unit for the push-in blower and the induction ventilator in a waste-carbonization pyrolysis melt-combustion apparatus having a power receiving facility for supplying required power to each part of the carbonization pyrolysis melting combustion apparatus. Using steam from Gas turbine and an electric motor directly connected thereto, an emergency power generator is further provided in parallel with the power receiving equipment, and a switching switchgear is provided on the load side of the power receiving equipment and the emergency power generator, and an electric power of the power receiving equipment is provided. In the event of loss,
The basic configuration of the present invention is that the required power is supplied from the emergency power generator to a rotary blower, an induction blower, a boiler feed pump, and a rotary driving device of a thermal decomposition drum via a switching opening / closing device. .

According to a second aspect of the present invention, in the first aspect of the present invention, a stationary rotation drive and an emergency rotation drive for supplying power from the emergency power generator are provided as the rotation drive of the thermal decomposition drum. It was made.

According to a third aspect of the present invention, in the first aspect of the present invention, the electric motor provided in the push-in blower and the induction ventilator is an induction motor, and is directly connected to the steam turbine when a large amount of steam is supplied from the waste heat boiler. The induction motor is an induction generator.

According to a fourth aspect of the present invention, in the first aspect of the present invention, an uninterruptible power supply for the pyrolysis gas burner is provided as a power supply for the pyrolysis gas burner of the melting and burning apparatus, and the uninterruptible power supply is combined with an emergency power generator. In parallel, power is supplied from the uninterruptible power supply to the pyrolysis gas burner until power is supplied from the emergency power generator.

According to a fifth aspect of the present invention, in the fourth aspect of the present invention, the uninterruptible power supply for the pyrolysis gas burner is formed by a thermoelectric element attached to a refractory outer wall of the melting and burning apparatus.

[0019]

Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is an overall system diagram of a waste distillation pyrolysis melting and burning apparatus according to an embodiment of the present invention. In FIG. 1, the same parts and members as those in FIGS. Reference numbers are used. In FIG. 1, 1 is a supply device, 2 is a dry distillation pyrolysis drum, 3 is a discharge device, 4 is a melting and burning device, 4a is a pyrolysis gas burner, 5 is a sorting device, 6 is a crushing device, and 7 is a waste heat boiler. , 8 is a dust collector, 9 is a gas purifier, 10 is a chimney, 11 is a heating tube,
2 is a hot-air generating furnace, 13 is a steam superheater, 14 is a steam turbine generator, 15 is a blower, 16 is an induced draft fan, 16a
Is an electric motor, 16b is a steam turbine, 17 is a cooling conveyor, 18 is a flammable fine powder storage tank, 19 is a heating gas passage, 2
0 is a circulation fan, 21 is a heat exchanger, 22 is a burner, 23
Is a waste pit, 24 is a waste supply crane, 25 is a gas duct, 26 is a forced blower, 26a is an electric motor, 26
b is a steam turbine, 31 is a power receiving facility, 32 is an emergency power generator, 33 is a switchgear, 34 is a load controller, 35
Is an uninterruptible power supply for the pyrolysis gas burner; 36 is a pyrolysis burner control device; a power receiving facility 31, an emergency power generation device 32, a switching device 33, a load control device 34, an uninterruptible power supply 35 for the pyrolysis gas burner. The other parts except the part of the pyrolysis burner control device 36 have the same configuration as those in the case of FIG. 2 and FIG.

Referring to FIG. 1, external power drawn into power receiving facility 31 and / or steam turbine generator 1
4 is supplied, and the push-in blower 26 and the induction blower 1 are switched via the switching device 33 and the load control device 34.
6. The required electric power is supplied to the rotary driving device 37 of the pyrolysis drum 2 and the like.

A so-called diesel generator is used for the emergency power generator 32. In this embodiment, the minimum power required to secure the safety stop of the plant, for example, the push-in blower 26, A boiler feed pump (not shown), an induction ventilator 16, a rotary driving device (minimum rotation speed) of the pyrolysis drum 2, an emergency power generation device 32 having a capacity capable of supplying electric power required by the pyrolysis gas burner 4a and the like are provided. Have been.

The pyrolysis burner control device 36 is provided with an uninterruptible power supply device 35 to prevent a power failure even when the main power supply is momentarily interrupted. In the present embodiment, a battery-type power supply is used as the uninterruptible power supply 35, which is connected in parallel with the emergency power supply 32, so that the emergency power supply 32 can be started up or switched. Even at the moment when the switching device 33 is operated, the pyrolysis gas burner 4a
Is supplied from the uninterruptible power supply 35 to the pyrolysis gas burner 4a so as not to extinguish the fire.

In this embodiment, the uninterruptible power supply 35
Although a battery-type power supply device is used as the power supply device, a thermoelectric element is used in place of the battery, and the thermoelectric element is attached to the refractory outer wall of the melting and burning device 4 to generate power using combustion heat. May be used.

Further, in addition to the rotary driving device 37 for normal operation, a small-capacity emergency rotary driving device 38 is provided on the pyrolysis drum 2 in order to secure the minimum rotation speed of the pyrolysis drum in an emergency. And a motor is used as a rotary drive.

The induction blower 16 and the push-in blower 26 are provided with a motor (induction motor 16
a, 26a) and steam turbines 16b, 26b, respectively, and the electric motor 16a and the steam turbine 16b, and the electric motor 26a and the steam turbine 26b are directly connected, respectively.

Next, the operation of the dry distillation pyrolysis melting and burning apparatus of the present invention will be described. At the time of steady operation of the plant, all electric power necessary for operation of each device and the like is supplied by external power and / or electric power from the steam turbine generator 14. The waste C stored in the waste pit 23 is sequentially supplied into the pyrolysis pyrolysis drum 2 by the supply device 1, and the heating pipe 11 is supplied with substantially no oxygen.
300 ℃ ～ 60 ℃ from normal temperature by heated gas K flowing inside
It is heated to a temperature of 0C, preferably 400C to 500C. By stirring and mixing for about 1 hour in this state, the waste C in the dry distillation pyrolysis drum 2 is pyrolyzed, and a pyrolysis gas G and a solid pyrolysis residue D are generated.

The thermal decomposition of the waste C is usually completed in about one hour, and about 75% by weight of pyrolysis gas G and 25% by weight of pyrolysis residue D are generated. In addition, the generated pyrolysis residue D is homogenized by being stirred and mixed in the dry distillation pyrolysis drum 2 to become particles of a uniform size. The generated pyrolysis gas G is mainly composed of water, CO, CO ₂ , H ₂ and hydrocarbons, and contains a small amount of dust and tar. The lower calorific value is about 1500-2
000 kcal / kg. Furthermore, the pyrolysis residue D is mainly composed of carbon and ash, but the carbon content varies depending on the particle size of the pyrolysis residue D, and the smaller the particle size, the higher the carbon content. For example, when the particle size of the pyrolysis residue D is 5 mm or less, the carbon content is approximately 35%.
wt%.

The pyrolysis gas G and the pyrolysis residue D in the dry distillation pyrolysis drum 2 are discharged into the adjacent carry-out device 3, where they are separated into the pyrolysis gas G and the pyrolysis residue D. The separated pyrolysis gas G is supplied to the melting and burning device 4 through the gas duct 25, and is so-called melt-burned together with the carbon residue I _O and the dust ash E described later. Further, the pyrolysis residue D is cooled from a temperature of about 400 ° C. to 500 ° C. to a temperature of about 80 ° C. on the cooling conveyor 17, and is a valuable material such as iron, aluminum or incombustible material in the sorting device 5. By sorting sand, glass, and the like, which are as described above, combustible solids I mainly composed of combustibles are separated. Further, the separated combustible solids I
After being pulverized by the pulverizer 6, it is stored as a carbon residue I ₀ in the combustible fine powder storage tank 18 and melted by pneumatic transport together with the dust ash E from the waste heat boiler 7 and the dust collector 8 as described above. It is sent to the combustion device 4 where it is burned together with the pyrolysis gas G. That is, the carbon residue I _O having a high carbon content supplied into the melting and burning device 4 is higher by 100 to 150 ° C. than the melting temperature of the ash in the melting and burning device 4 together with the dust ash E and the pyrolysis gas G. It is burned at a high temperature of about 1300 ° C., becomes molten slag F, flows down along the inclined bottom surface 4b, and is discharged from a slag discharge port 4d to a slag water-cooled conveyor (not shown). Become.

Approximately 1100 to 1100 generated in the melting and burning apparatus 4
The high temperature flue gas G _O of 1200 ° C. is sent to the waste heat boiler 7, and the flue gas G _O cooled to about 200 ° C. by heat recovery in the waste heat boiler 7 is subjected to dust removal by the dust collector 8. After the cleaning, the gas cleaning device 9 cleans the
After removing harmful substances such as SOx and SOx, NOx,
It is discharged into the atmosphere from zero.

If power from the outside or power from the steam turbine generator 14 cannot be received due to some accident or the like, the push-in blower 26 and the induction blower 16 are controlled by the steam turbines 26b and 16b. Normally driven for rotation for about 5 minutes. However, since the amount of steam generated by the waste heat boiler is reduced, it is difficult to perform normal rotation for more than 2 to 5 minutes only by driving the steam turbine. Therefore, the emergency power generator 32 is automatically started up within 5 to 40 seconds after the power cannot be received, and the switching device 33 is switched to the emergency power generator 3.
Automatically switched to 2 side. The emergency power generator 32
After the switching to the side, the steam turbines 26b, 16b and the induction motors 26a, 16a are operated in parallel, so that the driving force of the steam is reduced by the driving force of the motors 26a, 16b, while the push-in blower 26 and the induction fan are used. Each of the ventilators 16 is maintained in a steady operation state.

When the switchgear 33 is switched to the emergency power generator 32 during a power outage, equipment that needs to be operated in order to ensure the safety of the plant (for example, a boiler feed pump, a forced air blower 26, a pyrolysis drum, etc.) The power supply to all the components other than the emergency rotation drive device 38, the pyrolysis gas burner control device 36, and the induced draft fan 16) is cut off.

On the other hand, when the emergency power generation device 32 is started, power is supplied from the emergency power generation device 32 to the emergency rotation drive device 38 of the thermal decomposition drum 2 as described above. The rotation state can be switched to a low-speed rotation state of about 0.1 to 0.2 rpm because it is necessary to prevent a large expansion and contraction of itself. Further, at the time of a power failure, power is supplied from the uninterruptible power supply device 35 to the pyrolysis gas burner control device 36 until the emergency power generation device 32 is started. Therefore, the pyrolysis gas burner does not go into a fire extinguishing state.

Further, at the time of a power failure, the supply device 1 of the waste C to the pyrolysis drum other than the emergency load and the circulation fan 20 to the hot air generating furnace 12 are stopped, so that the generation amount of the pyrolysis gas G is also reduced. Decreases gradually. As a result, as the amount of steam generated in the waste heat boiler 7 decreases, the power consumption of the push-in blower 26 and the induction blower 16 increases, but as described above, the amount of generated pyrolysis gas G itself decreases. In addition, the power consumption of the forced air blower 26 and the induction blower 16 is significantly reduced as compared with the power consumption during the steady operation, so that the emergency power generator 32 can be small.

[0034]

According to the present invention, the thermal decomposition drum 2 is rotated at an extremely low speed by the emergency generator 32 at the time of a power failure, and the push-in blower 26 and the induction blower 16 are driven in combination by the steam turbines 26b, 16b. I have. As a result, the operation of the dry distillation pyrolysis melting and burning device can be stopped safely and smoothly at the time of a power failure with a relatively small-sized emergency power generator without requiring a large-capacity emergency power generator. The pyrolysis gas G generated by the residual heat after the power failure can also be completely burned, and environmental pollution caused by release of unburned substances and bad smell to the outside can be completely prevented.

When the dry distillation pyrolysis melting combustion apparatus is operated in a steady state, the induction motor directly connected thereto is driven by the push-in blower 26 or the steam turbines 26b, 16b of the induction ventilator 16, so-called induction power generation is performed. You may.
In this case, even if the equipment does not have the steam turbine power generator 14, it is possible to effectively use the waste heat.

Further, in the present invention, the pyrolysis gas G generated at the time of the power failure is completely burned in the melting and burning apparatus 4, so that the pyrolysis and pyrolysis and melting apparatus of the conventional waste is used. No auxiliary equipment such as an emergency combustion exhaust stack is required at all, and as a result, equipment costs and running costs can be significantly reduced. The present invention has excellent practical utility as described above.

[Brief description of the drawings]

FIG. 1 is an overall system diagram of an apparatus for dry distillation pyrolysis melting and burning of waste according to an embodiment of the present invention.

FIG. 2 is an overall system diagram showing an example of a conventional dry distillation pyrolysis melting and burning apparatus for waste.

FIG. 3 is a partial system diagram showing another example of the conventional dry distillation pyrolysis melting and burning apparatus for waste.

[Explanation of symbols]

1 is a supply device, 2 is a carbonization pyrolysis drum, 3 is an unloading device,
4 is a melting and burning device, 5 is a sorting device, 6 is a crushing device, 7 is a waste heat boiler, 8 is a dust collector, 9 is a gas purification device, 10 is a chimney, 11 is a heating tube, 12 is a hot air generator, 13 Is a steam superheater, 14 is a steam turbine generator, 15 is a blower, 16
Is an induction ventilator, 16a is an electric motor, 16b is a steam turbine, 17 is a cooling conveyor, 18 is a flammable fine powder storage tank, 1
9 is a heating gas passage, 20 is a circulation fan, 21 is a heat exchanger, 22 is a burner, 23 is a waste pit, 24 is a crane for supplying waste, 25 is a gas duct, 26 is a blower blower, 26a is a drive motor, 26b is a drive turbine,
27 is a switching device, 28 is an emergency combustion exhaust stack, 29 is a gas burner, 30 is a damper device, 31 is a power receiving facility, 32 is an emergency power generator, 33 is a switching device, 34 is a load control device, 35 is a pyrolysis gas burner. Uninterruptible power supply, 36 is a pyrolysis gas burner controller, 37 is a rotary drive for the pyrolysis drum for normal operation, 38 is an emergency rotary drive for the pyrolysis drum, C is waste, D is pyrolysis residue, K Is the heating gas, G
Is pyrolysis gas, G _O is combustion exhaust gas, I is flammable solid,
I ₀ is carbon residue, F is molten slag, and A is air for molten combustion.

Continued on the front page (51) Int.Cl. ⁷ Identification symbol FI Theme coat II (reference) F23G 5/00 ZAB F23G 5/027 ZABZ 4H012 115 5/16 ZABE 5/027 ZAB 5/20 ZABA 5/16 ZAB 5 / 44 ZABZ 5/20 ZAB B09B 3/00 ZAB 5/44 ZAB 302F 303H F term (reference) 3G081 BA02 BB00 BC07 BD00 DA14 3K061 AA23 AB02 AB03 AC01 BA06 CA01 CA07 DA02 DA12 DA17 DA19 DB18 FA10 FA27 GA06 KA02 AB02 AC01 BA06 HA01 HA03 JA05 JA18 3K078 AA06 BA08 CA02 CA13 CA21 4D004 AA46 BA03 CA08 CA24 CA29 CA32 CB09 CB34 DA02 DA03 DA06 4H012 HB03

Claims (5)

[Claims] 1. A dry distillation pyrolysis drum that pyrolyzes waste into pyrolysis gas and pyrolysis residue, a melt combustion device that melts and burns the pyrolysis gas and combustibles in the pyrolysis residue, and melt combustion A forced blower for supplying air for melting and combustion to the device,
A waste heat boiler that is provided downstream of the melt combustion device and recovers heat of flue gas from the melt combustion device, a gas purification device that purifies combustion exhaust gas from the waste heat boiler, and a gas purification device that is provided downstream of the gas purification device Dry distillation heat of waste with a draft fan, a chimney that releases combustion exhaust gas from the draft fan into the atmosphere, and a power receiving facility that supplies required power to each part of the dry distillation pyrolysis melting and burning device for waste In the cracking / melting / combustion apparatus, the push-in blower and the induction blower are each provided with a steam turbine using steam from a waste heat boiler and a motor directly connected to the steam turbine as a rotary driving device thereof, and further, in parallel with the power receiving equipment. And a switching switchgear provided on the load side of the power receiving equipment and the emergency power generator, and when the power of the power receiving equipment is lost, forced air blowing from the emergency power generator via the switchgear is provided. A carbonization pyrolysis melt combustion apparatus of waste, characterized by being configured as to supply a required electric power to the rotary drive of the induced draft fan and the boiler feed water pump and the pyrolysis drum. 2. The dry distillation pyrolysis of waste according to claim 1, wherein a rotary drive for the steady state and an emergency rotary drive for supplying power from the emergency power generator are provided as the rotary drive for the pyrolysis drum. Melt combustion equipment. 3. The induction motor according to claim 1, wherein the induction motor and the induction blower are provided as induction motors, and when the amount of steam supplied from the waste heat boiler is large, the induction motor directly connected to a steam turbine is used as an induction generator. 2. The apparatus for pyrolysis melting and burning of wastes according to claim 1. 4. An uninterruptible power supply for the pyrolysis gas burner is provided as a power supply for the pyrolysis gas burner of the melting and burning device, and the uninterruptible power supply is connected in parallel with the emergency power generator until power is supplied from the emergency power generator. 2. The dry distillation pyrolysis melting and burning apparatus for waste according to claim 1, wherein power is supplied from the uninterruptible power supply to the pyrolysis gas burner. 5. The dry distillation pyrolysis melting and burning apparatus for waste according to claim 4, wherein the uninterruptible power supply for the pyrolysis gas burner is formed by a thermoelectric element attached to a refractory outer wall of the melting and burning apparatus.