MXPA01003580A

MXPA01003580A - Multi-function treating device

Info

Publication number: MXPA01003580A
Application number: MXPA/A/2001/003580A
Authority: MX
Inventors: Maejima Takashi
Original assignee: Fumio Maejima; Maejima Takashi
Priority date: 1999-08-06
Filing date: 2001-04-06
Publication date: 2002-06-05

Abstract

A multi-function treating device for incinerating, drying, melting, decomposing and ash-melting untreated substances such as garbage, general rubbish, sludge and foamed polystyrene produced in factories, service providing facilities, wholesale markets, general business firms, general retail stores and households. The multi-function treating device comprises a dry-combustion furnace, kiln furnace, first flue, second flue, smoke combustion unit, dust collecting/filtering unit, second flue, air heating unit and cooling tank unit, characterized in that a unidirectional air flow from the cooling tank unit to the second flue is formed to maintain a negative pressure condition.

Description

MULTIFUNCTIONAL DESTRUCTION APPARATUS Field of the Invention The present invention relates to a multifunctional destruction apparatus for performing the destruction by incineration, drying, melting, degradation, ash melting and other functions, in an object to be destroyed such as raw garbage, general garbage, sediments, expanded polystyrene and other objects, produced in a manufacturing plant, a service provider, a wholesale market, a general company, a general store, a house and others.

Background of the invention Conventionally, an object that is going to be discarded, such as raw garbage and general garbage produced in a manufacturing plant, a service provider, a wholesale market, a general enterprise, a general store, a house and others, it is directly incinerated and dried in an incinerator. In addition, the object to be destroyed, such as sediment, is dried and then incinerated to be used as landfill, and expanded polystyrene (styrene foam) is collected to be degraded by a processor that has a special apparatus degradation by compression. However, because a general incinerator adopts a modality to send forced air to burn an object that is going to be destroyed, the repetition of the high and low temperature of the furnace, through the combustion of oxides, causes the smoke of combustion, and the escape of gases containing dangerous substances, such as dioxins. In addition, as incinerated ashes obtained from combustion also include hazardous substances, the ash generated from combustion can not be reused. That is, sediments, or raw waste containing a large amount of water, highly combustible paper or wood, paper bags from general stores, or plastic waste generate toxic gases, it can be said that a wrapping film transparent is the cause of the generation of dioxins, a plastic bottle, a general waste that can be burned, such as expanded polystyrene, are often put together in an incinerator, and a large water content decreases the combustion temperature, which accelerates the generation of dioxins.

There are incinerators, which prohibit the incineration of plastic bottles depending on the structure of the incinerators in the respective autonomous communities. In this case, the plastic bottles are separated to be collected. Therefore, it is an object of the present invention to provide a multifunctional destruction apparatus having functions in accordance with the types and uses subsequent to the destruction of an object, which is to be destroyed such as raw garbage, sediments, garbage generated , and an object based on polymers, such as expanded polystyrene produced in homes or businesses, for example, the apparatus has the capacity to perform the destruction by means of (1) microbial degradation, (2) pyrolysis, (3) drying low temperature, (4) indirect hot air drying, (5) direct drying by hot air, (6) carbonization, (7) incineration, (8) polymer melting and (9) ash melting. In other words, an object of the present invention is to provide a multifunctional destruction apparatus, which can dry the general garbage, the raw garbage, the sediments and other objects, which can not be incinerated when they contain large amounts of water; in the multifunctional destruction apparatus to be charred and incinerated regardless of its water content. Summary of the Invention The present invention provides a multifunctional destruction apparatus which comprises: a dry combustion furnace; a drying oven; a first portion of smoke feed; a second portion of smoke feed; a portion of smoke combustion; a filter portion for powders; a second portion of smoke feed; a portion of air heating; a cooling tank portion, wherein an air flow is generated in a direction from the cooling tank portion to a second smoke feed portion to obtain a vacuum condition.

BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a cross-sectional view showing a general multifunctional destruction apparatus according to the present invention; Figure 2 is an enlarged view showing a dry combustion furnace and a melting apparatus of the multifunctional destruction apparatus; Figure 3 is an enlarged view showing a drying oven, a first smoke feed portion, a smoke combustion portion, a dust filter portion and a second smoke feed portion of the multifunctional destruction apparatus; Figure 4 is an enlarged view showing the smoke combustion portion, and the dust filter apparatus of the multifunctional destruction apparatus; Figure 5 is an enlarged view of an air heating portion and a portion of the cooling tank of the multifunctional destruction apparatus; Figure 6 is a cross-sectional view showing a general multifunctional destruction apparatus according to another embodiment; Figure 7 is an enlarged view illustrating a drying oven, an ash casting portion and a smoke feeding portion of the multifunctional destruction apparatus according to another embodiment of the present invention; Figure 8 is a flow chart showing a method for pyrolyzing general refuse, or incinerated ash using the multifunctional destruction apparatus; Figure 10 is a flow chart illustrating an application method and a low temperature drying process in raw waste or sediments, using the multifunctional destruction apparatus; Figure 11 is a flow chart illustrating a method for using heated hot air to dry general waste, raw waste or sediments, using the multifunctional destruction apparatus; Figure 12 is a flow chart illustrating a method for using hot air, which is heated to dry general waste, raw waste or sediments, using the multifunctional destruction apparatus; Figure 13 is a flow chart illustrating a method for the carbonization of general waste, raw waste or sediments under a reduced atmosphere using a multifunctional destruction apparatus; Figure 14 is a flow chart illustrating a method for burning general waste, raw waste, sediment under a reduced atmosphere, using the multifunctional destruction apparatus; Figure 15 is a flow chart showing a method for casting expanded polystyrene, using the multifunctional destruction apparatus; Figure 16 is a flow chart showing a method for melting the incinerated ashes using the multifunctional destruction apparatus; Figure 17 is a partial cross-sectional view illustrating yet another embodiment of the multifunctional destruction apparatus in which a cylindrical tube for drying is provided, connected to a drying chamber; Figure 18 is a cross-sectional view illustrating the incorporation of the cylindrical tube for drying illustrated in Figure 17; Figure 19 is a cross-sectional view illustrating another embodiment of the cylindrical tube for drying; Figure 20 is a cross-sectional view illustrating yet another embodiment of the cylindrical tube for drying; Figure 21 is a partial cross-sectional view illustrating yet another embodiment of the cylindrical tube for drying; Figure 22 is a longitudinal sectional view of a check valve of one incorporated in Figure 21, illustrating the check valve being closed; Figure 23 is a longitudinal sectional view of the check valve incorporated in Figure 21, illustrating the check valve being open; Figure 24 is a partial cross-sectional view illustrating a further embodiment of a multifunctional destruction apparatus in accordance with the present invention; and Figure 25 is an enlarged view illustrating an air hole illustrated in Figure 21.

Detailed Description of the Invention A multifunctional destruction apparatus according to the present invention will now be described in detail, with reference to the accompanying drawings. A multifunctional destruction apparatus 1 according to the present invention includes: a dry combustion furnace 2; a drying oven 3; a first portion of smoke feed 4; a smoke combustion portion 5; a portion of dust filter 6; a second portion of smoke feed 7; an air heating portion 8; a portion of cooling tank 9; and a casting apparatus 10 (incinerated ash melting), The complete multifunctional destruction apparatus 1 is accommodated in a structure body 11 having an air intake box and is embedded in the ground under a ground 12, so that the outside air can be driven from the air intake opening llb. The air intake box Ia is connected to a burner, a fan, a heater, a combustion heating apparatus for liquid hydrogen and the like, provided for the dry combustion furnace 2, the first smoke feed portion, the portion of smoke combustion 5, the second smoke feed portion 7 and the air heating portion 8, so as to collectively allow the fresh air required for the combustion heating apparatus. The air intake opening llb is provided for the air intake box lia. A filter can be provided for opening the air inlet llb so that it does not absorb dust.

The multifunctional destruction apparatus 1 can not be embedded in the ground under the earth 12, but the respective devices from 2 to 10 can be installed directly in a plant or can not be installed without installing these devices from 2 to 10 in the field. of the structure 11. When the respective apparatuses of 2 to 10 are directly installed in a plant and the like, a protection plate d: 1 heat or the like can be provided around these apparatuses due to the extremely high heat they generate. In addition, an installation can be made to improve the permeability of the air. In Figures 2 through 5, a detailed description will now be provided as to what < cta to the respective devices from 2 to 10, as per e; For example, the dry combustion furnace 2, the drying furnace 3, the first smoke feed portion 4, the smoke combustion orifice 5, the dust filter portion 6, the second smoke feeding portion 7, j air heating portion 8, the cooling tank portion 9, and the casting apparatus (an incinerated ash melting apparatus). Figure 2 is a partially enlarged view of the multifunctional destruction apparatus according to the present invention, illustrating the dry combustion furnace and the casting apparatus, provided on the right side of the multifunctional destruction apparatus, taken along the length of line AA of Figure 1 in an enlarged manner. This apparatus adopts the method to perform the destruction, adjusting a temperature of a mixed waste material (expanded polystyrene, polymer, waste paper, raw waste, sediment and other objects), melting the polystyrene and drying the raw waste and sediment that subsequently they will be incinerated. The dry combustion furnace 2 includes a first dry chamber 15, a second dry chamber 15b, a third dry chamber 15d, a fourth dry chamber 15f and a combustion chamber (dry chamber) 17, from above in the order mentioned. A raw refuse / sediment input portion 13 is provided in the upper part of the first dry chamber 15, and a general refuse input portion 14 is provided in the upper part of the combustion chamber 17. The dry chambers 15, 15b, 15d, 15f, respectively, and the combustion chamber (dry chamber) 17, can not be formed separately in multiple stages but, they can be formed as a single camera. When the respective dry chambers 15, 15b, 15d, 15f and the combustion chamber (dry chambers) 17 are formed separately in multiple stages, production is improved. The raw garbage inlet portion 13 and the inlet portion of the general garbage 14, have the inlet openings 13a and 14a, which are open in a funnel-like manner respectively, and the first open / close valves 13b and 14b and the second opening / closing valves 13c and 14c are provided within said portions as illustrated in Figure 2. The first opening / closing valves 13b and 14b are used to move downward to the second valves of opening / closing 13c and 14c an appropriate amount of raw waste or sediment, and the general waste introduced by the entry openings 13a and 14a. The second opening / closing valves 13c and 14c introduce the raw waste, the sediment and the general waste together within the first dry chamber 15 and the combustion chamber 17. Needless to say, the waste material is not restricted only to raw garbage, sediment and other debris introduced in the entrance openings 13a, and that any garbage that can be burned and that can also be included any other object that is going to be destroyed, which has contained a large amount of water, but that has been dried. The general garbage is not restricted to that garbage introduced in the entrance opening 14a, but it can also be included any dry object that can be burned to be destroyed, which hardly contains water. Garbage having a large water content is introduced from the raw waste / sediment input portions 13 into the first dry chamber 15, and dried from the first combustion chamber to the fourth dry chamber (15, 15b, 15d) and 15f) in the order mentioned, to then be burned in combustion chamber 17. In addition, garbage that has no water content is not subjected to the drying process, but is introduced from the general garbage inlet portion 14 inside. of the combustion chamber 17 to be burned. In addition, a plurality of dry plates 15a are placed so that they have the ability to rotate on the bottom face of the first dry chamber 15. As illustrated in Figure 2, the dry plates, similar to long plates 15a are provided. so that they can rotate around an arrow. When all the dried plates 15a are oriented in the horizontal direction, the raw garbage or the sediment can be mounted in the dry chambers 15a. On the other hand, all the dry plates 15a rotate in orientation of the vertical direction, the raw garbage, the sediment and the like can be moved downwards, inside the second dry chamber 15 from the openings between the respective dry plates 15a. The raw garbage, the sediment and the like, mounted on the dry plates 15a are dried by hot air originating in the second dry chamber 15b on the lower side of the first dry chamber 15. Of course, an opening can be formed and placed between the respective dry plates 15a or between the dry plates 15a and the surface of the wall. The dry plates 15a can rotate 180 degrees. The back sides of the dry plates 15a can also be used, and both the front surface and the back surface can serve as dry plates. Both surfaces are alternately used to prevent the dry plates 15a from being deformed by heat. When the dried plates 15a, and the grate plates 15c, 15e and 15g rotate 180 degrees, the raw garbage, the sediment and other debris, can be expelled uniformly. In a manner similar to the first dry chamber 15, a plurality of grating plates 15c are placed, which have the ability to rotate on the bottom face of the second dry chamber 15b; the grid plates 15e having structures similar to those provided in the third dry chamber 15d; and the 15g grid plates have structures similar to those provided in the fourth dry chamber 15f. Of course, the grid gratings 15c, 15e and 15g respectively, may have a rotating structure, or a fixed structure which does not allow rotation or turns. When the respective grid plates 15c, 15e and 15g rotate or rotate around the arrow, the raw refuse, sediment and other objects found in the respective dry chambers 15b, 15d and 15f can be caused to fall into the chambers lower dryers 15d, 15f or to the combustion chamber 17. In order to cause the raw garbage, sediment and other objects to fall into the second dry chamber, the fourth dry chambers 15b, 15e and 15f and the combustion chamber 17, in the order mentioned, they provide plural dry plates 15a or multiple grid plates 15c, 15e and 15g, which are not a plate that makes uniform agitation possible when raw refuse, sediments and other objects fall, thereby drying uniform. As illustrated in Figure 2, the width between the respective gratings of the grid plates 15c, the grid plates 15e and the grid plates 15c is different, that is, an opening between the grids of the grid plates 15c is the most important. narrow an opening between the grids of the grate plates 15e is larger than an opening between the grids of the grate plates 15c; and an opening between the grids of the grate plates 15c is greater than an opening between the grids of the grate plate 15e. This is because the raw garbage, the sediment and other debris, which fall down, are gradually dried in the second dry chamber 15b, the third dry chamber 15d and the fourth dry chamber 15e in the order mentioned, as they fall . These become fine particles that have no water content, and the raw garbage, sediment and other objects, dried on the upper faces of the grate plates 15c, 15e and 15g pass from there, through the space between the grids, to fall into the lower dry chambers without rotating the dry plates. The raw garbage, sediments and other objects that have passed from the first dry chamber 15 to the fourth dry chamber 15f to be dried and the general garbage introduced from the general garbage inlet portion 14 are collected in the combustion chamber 17 provided under the fourth dry chamber 15f. A fire grate 17b is provided on the bottom face of the combustion chamber 17, and the garbage is mounted on the fire grate 17b. A heating chamber 20 for housing the air heated by the heating burner 20a, and the heat radiator tube 20b connected to the heating chamber 20 are provided below the combustion chamber 17; an air guide tube 19 for sending fresh air to the heating burner 20a is connected to the heating burner 20a; an exhaust pipe 21 for emitting the hot air in the heat radiator tube 20 inside the outside of the dry combustion furnace 2, is connected to the heat radiator tube 20b, and an air supply pipe 22 is connected to take hot fresh air, or fresh air to the oven 2. A plurality of thermal storage means 20c consisting of ceramic, or a heat-resistant metal is provided in the heating chamber 20. When the thermal storage means 20c is heated by the heating burner 20a, the heat of the heating burner 20a is stored. In addition, when the heating is carried out beyond the capacity of the thermal storage means 20c, infrared rays or heat are emitted, so that the heating chamber 20 can be maintained at a high temperature. The air guide tube 19, and the exhaust pipe 21 communicate with the air intake box Ia adapted to the body of the structure 11 of the multifunctional destruction apparatus 1. As illustrated in Figure 5, an open / close valve 22a is connected to the pipe. of air supply 22, and connected to both is the air supply tube 58 of the first air heating portion 8 and an air cooling tube 61 of the cooling tank portion 9 so that the air fresh heated or chilled fresh air, or mixed air of hot fresh air, and cold fresh air can be conducted inside dry combustion furnace 2. Air supply pipe 22 to take in hot fresh air or fresh air it is connected because fresh air is sent from the air-conducting tube 19 to the heating burner 20a, but the oxygen for incineration is hardly contained by the air heated by the heating heater. or 20a. The heat radiator tube 20b does not directly send the hot air through the heating burner 20a into the combustion chamber 17, but heats the fresh air around the heat radiator tube 20b due to the heat of the heat radiator tube 20b to transmit to the high heat to the combustion chamber 17. When the combustion chamber 17 is also dried simultaneously by the indirect heat, the heat emitted by the heat radiator tube 20b and the fresh air can dry the garbage in the combustion chamber 17 to a high temperature and hot air from the heat radiator tube 20b, and the heat for drying the garbage can dry the raw garbage, or the sediment in its path from the first dry chamber 15 to the fourth dry chamber 15f. The smoke generated by the hot air from the heat radiator tube 20b and the incineration of the garbage is expelled to a smoke exhaust pipe 29 connected to the upper portion of the first dry chamber 15. An opening / closing valve is provided. 29a in the middle part of the main smoke pipe 29, and the main smoke pipe 29 is connected to the drying oven 3. The drying oven 3 can be connected to the dry combustion furnace 2. As illustrated in the Figure 3, the dry combustion furnace 2 is connected to the drying oven 3 through the smoke conduit 29, and the drying oven 3 is connected to the first smoke feed portion 4. When the fan 39 is operated to send Forced air from the tip 39b of the air supply tube 39a of a duct 40, the interior of a centrifugal furnace 35 of the first smoke feed portion 4 forms a vacuum, and the air or smoke from the combustion furnace dry 2, it is abso Thus, as the interior of the dry combustion furnace 2 also forms a vacuum, fresh air is absorbed from the air supply tube 22. As illustrated in FIG. Figure 2, a vibrator 17a is provided for the fire grate 17b seated at the bottom of the combustion chamber 17. Upon finishing the incineration of the garbage in the combustion chamber 17, the vibrator 17a is operated to vibrate the grate for fire 17b, so that the incinerated ash resting on the fire grate 17b can be sent to an ash tray 17c. The fire grate 17 can have a structure that allows a vibrator 17a to adhere thereto, as well as rotation. In addition, a belt conveyor can be placed in place of the ash tray 17c. As illustrated in Figure 2, the lower portion of the heat radiator tube 20b is provided with a funnel ventilation tray 23 for collecting the funnel ventilation generated by the incineration of the waste, or funnel ventilation and the like, produced when the dry combustion furnace 2 is used as a carbonization apparatus. As illustrated in Figure 2, the doors 16, 16a and 18, which can be opened / closed for cleaning, to remove debris, maintenance or inspection, to confirm the combustion conditions, are placed in the first dry chamber 15, the third dry chamber 15d, the fourth chamber dry 15f and the combustion chamber 17 and other components. Also provided is an ash access door 18a for receiving or removing the ash pan 17c and a funnel vent access door 24 for receiving or removing the funnel ventilation pan 23, and other components. Wheels and rails can be provided on the inner surfaces of the ash tray 17c, the funnel ventilation tray 23 and other components, so that the ash tray 17c and the funnel ventilation tray 23 can be introduced or removed from it. the ash access door 18a and the funnel ventilation access door 24, in order to remove the ash, or send the funnel ventilation to the outside of the combustion chamber 2.

A circulation tube 30 is provided to utilize the combustion heat generated from the incineration of the garbage for the combustion chamber 17, as illustrated in Figure 2. The circulation tube 30 is connected to the circulation tube 30 of a machine. freezer 63. The circulation tube 30 is used to operate the freezing machine 63 employed in the portion of the cooling tank 9 that is, which filters the water and operates the freezing machine 63, using water or high temperature steam. As illustrated in Figure 2, a belt conveyor can be provided in the inlet openings 13a and 14a of the raw waste / sediment input portion 13, and in the general refuse input portion 14 so that Raw waste, sediment, general waste and other objects can be transported automatically and introduced into the entry openings 13a and 14a. All valves 13b, 13c, 14b, 14c, 22a and 29a are provided for the dry combustion furnace 2, and all the grate plates 15a, 15c, 15e and 15g, the fire grate 17b, the vibrator 17a and the heating burner 20a can be automatically controlled by a computer or similar equipment. Sensors can be installed to detect the combustion temperature, an expulsion temperature, a water content and other measurements, in the dry chambers 15, 15b, 15d and 15f, the combustion chamber 17, the heating chamber 20 and other components to make automatic control possible using the computer. The casting apparatus 10 is composed of an air supply pipe 25, a casting tank 26, an exhaust pipe 28 and other components. A tray 26b is provided under the smelting tank 26, and a grid plate 26a, for collecting the polyethylene foam or polymer-based substances on top of the tray 26. The expanded polystyrene (so-called expanded polystyrene) and polymer-based substances and the like 27, are placed on the upper face of the grid plate 26a, and an open / close valve 25a is provided for the air supply tube 25, which is open to conduct the hot air supplied from the heating portion. of air 8 inside the smelting tank 26. When the heat is transmitted from the wall of the dry combustion furnace 2 used for the casting, only a small amount of hot air coming from the heating portion 8 is profitably required. As the hot air conduction has an extremely high temperature, it melts the expanded polystyrene, the polymer substance and the like 27, and the melted liquid substances are deposited in the tray 26b. A polystyrene agglomerate, which is the melted substance conserved in the tray 26, is the polymer-based substance, and is therefore suitable for re-use. The hot air that has melted the expanded polystyrene, and the polymer-based substance 27 passes through the exhaust pipe 28 having an opening / closing valve 28a, to be fed to the second smoke feed portion 7. As illustrated in Figure 3, these are substances are burned in the burner 50 at an extremely high temperature and incinerated again in the centrifugal furnace 48. Subsequently, it is quickly used to be expelled from the funnel 53, to the outside of the second smoke feed portion 7. It can be used a computer or similar equipment for automatically controlling the operation of the opening / closing valves 25a and 28a provided for the casting apparatus 10. A sensor for detecting a temperature and the like can be provided in the casting tank 26 to allow control automatic using a computer. Figure 3 is a partially enlarged view of a multifunctional destruction apparatus according to the present invention. That is, it is an enlarged view showing the drying oven 3, the first smoke feed portion 4, the smoke combustion chamber 5, the dust filter portion 6 and the second smoke feeding portion 7, provided between line AA and line BB of Figure 1. Figure 4 is an enlarged view of the smoke combustion portion, and the dust filter portion of the multifunctional destruction apparatus according to the present invention. Referring to Figure 3, the smoke guide tube 29 connected to the dry combustion chamber 2, illustrated in Figure 2 is continuously provided to the drying oven 3, the first smoke feed portion 4, the portion of smoke combustion 5, the dust filter portion 6 and the second smoke feed portion 7, in the order mentioned. The drying oven 3 has rotatably adapted a tip 31a of the smoke pipe 29 and an end 31b of the centrifugal furnace 35. A plurality of rails 31c are provided for the peripheral outer surface of the cylindrical body 3 of the drying oven 3. Also found are the driving wheels 31d, which rotate in contact with the rails 31c of the cylindrical body 31. A storage chamber 33 for the drying oven 3 is provided by means of the tube 33a and an opening / closing valve 34 between the centrifugal furnace 35 and the drying oven 3. The reference number 32 indicates a garbage inlet portion, for introducing the garbage into the cylindrical body 31 of the drying oven 3. The garbage inlet portion 32 and the garbage inlet portion 32 can be provided. storage chamber 33 for the burnt residues, in the opposite positions on the surfaces of the left side and right side. The garbage inlet portion 32 provided for the drying oven 3 has an inlet opening 32a, open in a funnel-like manner, and a first open / close valve 32b and a second open / close valve 32c are provided. in the garbage inlet portion 32, as illustrated in Figure 3. The first opening / closing valve 32b is used to drop an appropriate amount of raw garbage, sediment and general garbage and others that have entered. from the entry opening 32a into the second opening / closing valve 32c, and the second opening / closing valve 32c is used to introduce the raw waste, the sediment, the general waste and other objects into the drying oven 3. The cylindrical body 31 of the drying oven 3 is hollow, and the hot air and smoke flowing inside the rotating cylindrical body 31 is sent dry from the smoke pipe 29 and incinerates the object to be burned, m the garbage in the drying oven 3. The exhaust gas, hot air, smoke and duct gas generated by the incineration are absorbed into the first portion of the smoke feed 4. The burned embers obtained by the drying and incineration of the combustion object, while rotating in the cylindrical body 31, rotate in the storage chamber 33 through the tube 33a. Burned embers can be reused as fertilizers and other uses, because they are completely burned at an extremely high temperature. The opening / closing of all valves 29a, 32b, 32c and 34 provided for the drying oven 3, and the rotation of the cylindrical body 31 by the driving wheels 31d can be controlled automatically by a computer or similar equipment, sensors can be provided to detect the combustion temperature, a temperature of leakage and water content and other measurements, for the interior of the cylindrical body 31, the smoke pipe 29 and other components, in order to make automatic control possible using a computer. The first smoke feed portion 4 is formed by a centrifugal furnace 35, an air-conducting pipe 36, a burner 37, an air supply pipe 38, a fan 39, an air supply pipe 39a and a pipe 40 Because the tip of the air supply tube 39a adhered to the fan 39 is inserted slightly into the end of the tube 40a of the conduit 40, the air supplied from one end of the tube 39b of the air supply tube 39a connected to the fan 39 , is blown from the lower end 40a of the duct 40, and is further emitted to the duct 40 while admitting the smoke, hot air and other emissions from the interior of the centrifugal furnace 35, by means of the effect of the ejector. Therefore, the interior of the centrifugal furnace 35 constantly forms a vacuum. The hot air, smoke and other emissions from the drying oven 3 are blown to a position changed slightly from the center of the upper portion of the centrifugal furnace 35 and cause a funnel ventilation contained in the hot air, smoke and other emissions, are gradually expelled into the lower portion of the centrifugal furnace 35, while spiraling in the centrifugal furnace 35. At this time the burner 37 attached to accelerate the spiral rotation of hot air, smoke and other emissions, returns to heat the funnel ventilation contained in hot air, smoke and other emissions, so that the ventilation of the funnel is completely burned to be non-toxic. A vortex flow in the centrifugal chamber 35 extremely extends the flame of the burner 37, and the hot air and some of the other substances that are in contact with the flame for a prolonged period of time (a retention time of not less than 100% is required). 2 seconds, with respect to a newly constituted furnace, in accordance with the secondary instructions of the Waste Management Law issued in January 1997). Therefore, the interior of the centrifugal furnace 35 can maintain a high temperature or a ceramic heat retaining material can be provided inside to maintain a high temperature by the effect of thermal storage. (In the aforementioned guide, an incineration temperature of not less than 850 ° C, or preferably not lower than 900 ° C is required) For the incineration of PCBs a temperature of 1100 ° C or higher has been designated). In addition, because the air supply tube 38 for driving fresh air into the fan 39 is connected to the air guide tube 60 which passes through the cooling tank portion 9, the air conducted to the fan 38 is required. becomes an extremely cold air capable of cooling the high temperature hot air in the centrifugal furnace 35 in a burst, in order not to recombine the dioxins at a temperature of about 300 ° C (it is said that the rapid cooling of the the combustion gases should not be at a temperature higher than 200 ° C, there is a research result that mentions that cooling is necessary at a temperature not exceeding 200 ° C in about one second). Therefore, toxic substances, such as dioxin, Nox, SOx, HCl and others contained in hot air, smoke and other emissions, can be pyrolyzed in the centrifugal furnace 35 to remove smoke, dust and other emissions. The air guide tube 36, and the air supply tube 38 connected to the burner 37 and the fan 39, have their smoke ends connected to the air intake box llia to admit fresh air. In addition, the gas conduit 40 adhered to the centrifugal furnace 35 of the first smoke feed portion 4, is connected to the smoke combustion portion 5. The operation of the burner 37 and the fan 39 provided in the first feed portion of Smoke 4, can be controlled automatically by a computer. In addition, sensors are connected to detect a combustion temperature, an exhaust temperature, a water content and other measurements, in the centrifugal furnace 35, in order to allow automatic control by a computer. In the multifunctional destroying apparatus according to the present invention, the drying oven 3 may not be provided. The drying oven 3 may be provided in front of the dry combustion furnace 2. In the multifunctional destruction apparatus according to the present invention , the dry combustion furnace 3 may not be provided. The description of the smoke combustion portion 5, and the dust filter portion 6 shown in Figure 4 will now be provided. As illustrated in Figure 4, the Smoke combustion portion 5 again burns the hot air, smoke and gas at a high temperature, which are emitted by the first smoke feed portion 4, and are substantially deactivated, so that they are completely burned. The smoke combustion portion 5 is composed of a gas conduit 40, a catalytic burner 41, a catalytic auxiliary burner 42, an air conducting tube 43, an air intake box 43a, and a heating burner 43b. The catalytic burner 41 is a cylindrical body provided between the gas conduits 40 and 44. In order to accept toxins and toxic gases from the auxiliary catalytic heater 42, a preliminary heating is required to produce a high temperature, in which the dioxins and the toxic gases are burned, the catalytic heater 41 is provided with the auxiliary catalytic heater 42. In order to burn the gas fed at an extremely high temperature, the catalytic burner 41 and the auxiliary catalytic burner 42, include the nozzles 41a and 42a for spraying kerosene, crude oil or gas and the like; the mixers 41b and 42b for burning the mixed gases; the thermal catalysts 41c and 42c, and the ceramic 41d and 42d. The nozzles 41a and 42a for spraying kerosene, crude oil or gas and the like, can be stoves or heaters. In addition, kerosene, crude oil or gas and the like, and liquid hydrogen can be sprayed. The following is the same as the previous. The fresh air is admitted from the air guide tube 43 connected to the air intake box Ia inside the heating burner 43b and the auxiliary catalytic burner 42. In the heating chamber 42e, the heat generated by the combustion of the burner is retained. of heating 43b, fresh air taken from auxiliary catalytic burner 42 is heated, kerosene, crude oil or gas and the like, are sprayed into fresh air heated by nozzles 42a to form a mixed gas of heated fresh air and gas sprayed A plurality of thermal storage means 42f consisting of ceramic, heat resistant metals and other materials are provided within the heating chamber 42e, heating of the thermal storage means 42f by the heating burner 43b causes the heat of the heating burner 43b is stored. When heating has been performed beyond the capacity of the thermal storage means 42f, an infrared ray or heat is emitted to maintain the heating chamber 42e at a high temperature. A temperature of the mixed gas of the heated fresh air and the dew gas increases the flash point to start the combustion, and the mixed gas passes to the mixer 42b to be further mixed. The gas mixed in the combustion condition is subjected to catalytic combustion by passing it through the thermal catalyst 42c. After passing the thermal catalyst 42c, the mixed gas is converted to a high temperature thermal catalytic gas having a temperature of about 800 ° C to 1300 ° C. The high temperature thermal catalytic gas passes through the ceramic 42d having a honeycomb structure, to be supplied to the catalytic burner 41. In the catalytic burner 41, the gas passing to the pipe 40 by means of the first feed portion of smoke 4, is mixed with the high temperature thermal catalytic gas, and is sprayed with kerosene, crude oil, gas or liquid hydrogen, or burned to form a mixed gas. The temperature of the mixed gas increased to a flash point (from about 200 ° C to 250 ° C) to start combustion, and the gas is well mixed, as it passes through the mixer 41b. The gas mixed in the combustion condition is subjected to catalytic combustion at a temperature of about 400 ° C by passing it through the thermal catalyst 41c. The mixed gas then passes through the thermal catalyst to become a high temperature thermal catalytic gas, having a temperature of about 800 ° C to 1300 ° C. The high temperature thermal catalytic gas passes through the ceramic 41d which has a honeycomb structure, to be fed to the gas conduit 44. The gas passing through the catalytic heater 41 is subjected to complete combustion like the catalytic gas High temperature thermal, and the exhaust gas emitted to the gas conduit, becomes a complete combustion gas containing a tiny amount of dust. Toxic substances, such as dioxins, toxic gases, NOx, SOx, HCl and other substances, are completely decomposed and removed from the combustion gas. The powder contained in the exhaust gas is filtered by the powder filter portion 6 provided between the gas conduits 44 and 47. The dust filter portion 6 is divided between the gas conduit allowing the passage through the apparatus of the dust filter 46 and the gas conduit 45, which does not allow passage through the dust filter apparatus 46. The filter apparatus is provided with the purpose of allowing passage through the gas conduit 45., controlling the opening / closing valves 44a and 45a when the complete flue gas is obtained after passing through the smoke combustion portion 5, does not contain dust or when it is not provided, or the dust filter is not operated 46. The multifunctional destruction apparatus 1 may not contain this dust filter apparatus 46. As is generally known, that combination dioxins have the tendency to advance using funnel ventilation in the exit gas as a catalyst, during the Exhaust gas cooling, the combustion smoke is maintained at a high temperature by the catalytic burner 41 of the smoke combustion portion 5 to completely oxidize and decompose the dioxins. Subsequently, funnel ventilation in the exhaust gas is removed before rapid cooling in the centrifugal furnace 48 of the second smoke feed portion 7. This is a very effective means. The dust filter apparatus 46 is constituted by a filter, a semi-automatic filter, an electric dust collector, a wet dust collecting apparatus, a spray tower and other components. The dust filter apparatus 46 has a structure made of a combination of some or all, the filter, the semi-automatic filter, the electric dust collector, the wet dust collecting apparatus, the spray tower and other components. A combination of these elements to constitute a dust filter apparatus 46 can be changed to be used with intake components and the like, of an object to be incinerated, such as the garbage to be destroyed that is being taken in consideration The filter is obtained from the formation of dust, particles or sponge, or the molding of burned lime, calcium hydroxide and activated carbon in a plate, so that it is superimposed in the form of layers. This filter transmits exhaust gas through the layers of burned lime, calcium hydroxide and activated carbon to remove funnel ventilation and toxic gas. The semi-automatic filter has the ability to collect fine particles by means of a collector apparatus for collecting fine dust, using a bag of filter material and the like, and is often used in an electric vacuum cleaner and the like. Since the temperature of the exhaust gas is extremely high, the material of the bag of filter material must be carefully selected. In particular, when the temperature is too high for the filter material, water must be sprayed, injected or applied in the form of drops, from a nozzle to lower the temperature of the exhaust gas. The electric vacuum cleaner is an apparatus for collecting the fine particles in an electrode plate by the static charging force and is often connected to an exhaust pipe of a plant and the like. This is a machine that generates a corona discharge in it, and applies funnel ventilation to the negative pole to be collected at the positive pole. The wet dust collection device rapidly lowers the temperature while removing the impurities by spraying or injecting water into the exhaust gas containing the dust and is called a scrubber. It is used to purify the components that are soluble in water, of which there is a small amount in the exhaust gas. A centrifugal cleaner can be used to collect the funnel ventilation causing the dust contained in the exhaust gas, which moves upward spirally in the cylinder, to collide with liquid droplets sprayed from the center of the cylinder into the cylinder. radial direction or a fluid bed scrubber, which collects the funnel ventilation by dropping liquid from the upper nozzle, while causing the hollow synthetic resin, similar to a table tennis ball in the form of a filler, to make it float by the flow of the exhaust gas. The dew tower is an application of the scrubber, which removes funnel ventilation by dispersing liquid droplets, liquid films or bubbles of a cleaning liquid from multiple nozzles in a direction opposite to the dust containing the exhaust gas flow, and is called a cooling tower. Because the time the liquid droplets are in contact with the exhaust gas is long, the ratio to remove toxic gases or funnel ventilation becomes higher, and this tower is often used in a small incinerator . An opening / closing valve 47a is connected to a gas conduit 47 connected to the dust filter apparatus 46, and an exhaust pipe 28 of the melting apparatus 10 is connected to the rear portion of the opening / closing valve 47a. When the casting apparatus 10 is operated, the hot air used to melt the expanded polyethylene and the polymer-based substances at a high temperature is supplied to the gas conduit 47. When the gas that has passed through the dust filter portion 6 in the second smoke feed portion 7 is being burned again, the opening / closing valve 28a of the exhaust pipe 28 is closed and the opening valve / Closing 47a of the gas conduit 7 is open. When the hot air is also re-burned in the second smoke feed portion 7, which has passed through the casting apparatus 10, both opening / closing valves 28a and 47a are opened. All the valves 44a, 45a and 47a, the heating burner 43b, and the nozzles 41a and 42a connected to the smoke combustion portion 5 and to the dust filter portion 6 can be automatically controlled by a computer. Various types of sensors can be supplied to detect a combustion temperature, an exhaust temperature, a water content and other measurements, in the gas conduits 40 and 44, the catalytic burner 41, the auxiliary catalytic burner 42, and the apparatus of dust filter 46 and other components, to allow automatic control by a computer. As illustrated in Figure 3, the gas conduit 47 of the dust filter portion 6 is connected to the centrifugal furnace 48 of the second smoke feed portion 7. The second smoke feed portion 7 is formed by the furnace centrifugal 48, the air guide tube 49 for admitting air, the burner 50, the air tube 51, the fan 52, the air supply tube 52a and the conduit 53. As the tip of the air supply tube 52a Adhered to the fan 52 is inserted slightly into the lower end 53a of the conduit 53, the air supplied from the tip 52b of the air supply tube 52a connected to the fan 52 is blown to the lower end 53a of the conduit 53, and the air is emitted at the conduit 53 while admitting smoke, hot air and other emissions in the centrifugal furnace 48, by ejector effect. Therefore, the interior of the centrifugal furnace 48 forms a vacuum constantly. A method can be used to insert a tube directly into the duct and supply the air through the fan to keep the air in the oven in a vacuum. Alternatively, an induction fan can be used. In addition, as illustrated in Figure 3, gas such as hot air, smoke and other emissions generated from the dust filter portion 6 or the casting apparatus 10 is blown to a slightly changed position from the center of the part of the centrifugal furnace 48 and gradually moves down the funnel vent contained in the hot air or the smoke that is to be blown downwards while rotating in the centrifugal furnace 48. Here, the burner 50 adhered to accelerate the direction of Rotation of hot air or smoke is used to burn the gas again, so that the gas can be subjected to a complete combustion so as not to be toxic. The swirl flow in the centrifugal furnace 48 ensures that the flame of the burner 50 is extended extremely, and the hot air and smoke can be brought into contact with the flame for a long period of time, thereby maintaining the interior of the centrifugal furnace 48 at a high temperature. Further, since the air tube 51 for driving fresh air into the fan 52 is connected to the air guide tube 60 passing through the cooling tank portion 9, the air conducted inside the fan 52 becomes very cold air , and the hot air maintained at a high temperature in the centrifugal furnace 48 can be cooled in a burst. Therefore, toxic substances such as dioxins, NOx, SOx, HCl and others, contained in hot air or smoke can be completely pyrolyzed in the centrifugal furnace 48, and smoke, dust and others can be completely removed at the final . The air guide tube 49 and the air tube 51 connected to the burner 50 and the fan 52 have their ends in communication with the air intake box Ia, so that the fresh air can be admitted. In addition, the conduit 40 leaves from the centrifugal furnace 48 to the exterior of the multifunctional destruction apparatus 1 and discharges the non-toxic non-molten gases to the exterior of the apparatus 1. The operation of the burner 50 and the fan 52 connected to the second supply portion Smoke 7 can be controlled automatically by a computer. Sensors can be provided to detect a combustion temperature, an exhaust temperature, a water content, a vacuum condition, a smoke and other measurements, in the centrifugal furnace 48 to allow automatic control by a computer. Figure 5 is a partially amplified view of a multifunctional destruction apparatus according to the present invention, illustrating the air heating portion and the cooling tank portion that is on the left side of the multifunctional destruction apparatus, taken along the line BB of Figure 1 in an enlarged manner. The air heating portion 8 includes the air guide tube 54, the heating burner 55, the air tube 56, the heating chamber 57 and the air supply tube 58. The fresh air conducted from the conductive tube of air 54, whose end is inserted into the air intake box Ia is used for the combustion of the heating burner 55 connected to the other end of the air guide tube 54. The heating burner 55 is installed in the heating chamber 57 and heats the admitted fresh air from the air tube 56 connected to the air intake box lia. Then, the hot air is absorbed by the air supply tube 58 due to the vacuum condition. A plurality of thermal storage means 57a of ceramics, heat resistant metals and other materials are included in the heating chamber 57. When the heat storage means 57a is heated by the heating burner 55, the heat of the heating 55 is stored. Also, when the heating is carried out beyond the capacity of the thermal storage means 57a, an infrared ray or heat is emitted, thereby maintaining the heating chamber 57 at a high temperature. The air supply tube 58 is connected to an air cooling tube 61 of the cooling tank portion 9, the air supply tube 22 of the dry combustion furnace 2, and the air supply tube 25 of the apparatus casting 10. The hot air supplied from the heating chamber 57 to the air supply tube 58, is absorbed into the air supply tube 22 of the dry combustion furnace 2 and the air supply pipe 25 of the casting apparatus 10. When the hot air is supplied to the air supply pipe 22 of the dry combustion furnace 2, the cold air or the gas which is a mixture of the hot air and the cold air having an average temperature, it can also be supplied to hot air. Therefore, the temperature of the gas supplied to the air supply tube 22 can be adjusted by controlling a trip of the opening / closing valve 61b of the air cooling tube 61. Of course, the adjustment of the amount of heating of the burner of heating 55 of the air heating portion 8 or travels of the opening / closing valve 58a of the air supply tube 58, the opening / closing valve 22a of the air supply tube 22, the opening valve / 61b closure of air cooling tube 61 can be automatically controlled by a computer. Sensors can be provided for the detection of a combustion temperature, a temperature, a water content, a vacuum condition, a smoke and other measurements in the heating chamber 57, the air supply tube 22 and other components to allow Automatic control by a computer. The cooling tank portion 9 is composed of a water tank 59, an air guide tube 60, an air cooling tube 61, an endothermic tube 62, a circulation tube 30, a freezing machine 63, and a tube 64. The inlet opening 59a through which water, rainwater, snow, ice and other liquids can be introduced into the water tank 59, is provided in the upper part of the water tank 59, a opening / closing valve 59a for adjusting an amount of water or ice, which can be introduced into the water tank 59. The air guide tube 60 and the air cooling tube 61 communicate with the water tank 59. The air guide tube 60 conducts fresh air inside the fan 39, which demonstrates the effect of the ejector of the first smoke feed portion 4, and the second smoke feed portion 7, and a part of the air guide tube 60 What dry municates with the water tank 59 which is provided with a cooling portion 60a positioned in a corrugated manner, so that the fresh air to be conducted to the fans 39 and 52 can be cooled. The air cooling tube 61 is used to drive the fresh air to the dry combustion furnace 2. This tube 61 is provided for the purpose of lowering the temperature of the heated air heated by the air heating portion 8 to be driven into the air. dry combustion furnace 2 or absorb the dry cold air inside the dry combustion furnace 2. The cooling portion 61a is connected to the air cooling tube 61, which is positioned in a corrugated form in the portion communicating with the water tank, and opening / closing valve 61b, so that cold air and cool fresh air driven inside the dry combustion furnace 2 can be supplied while adjusting the amount thereof. As cold air can be absorbed by forming a vacuum in the furnace, the uniform supply of air in the furnace can be used. In order to cool the water or liquid stored in the water tank 59, the endothermic tube 62 connected to the cooling machine 63 is placed in the water tank 59. A cooler having a low coagulation point is circulated. which is cooled in the freezing machine 63 in the endothermic tube 62, and this cooler admits the heat of the water or the liquid in the water tank through an endothermic tube 62 to cool the water or liquid. The circulation tube 30 connected to the combustion chamber 17 of the dry combustion furnace 2 is connected to the freezing machine 63 to transmit the combustion heat obtained from the combustion chamber 17 for the freezing machine 63 using hot water, steam and other in the circulation tube 30. The heat of combustion is used in the freezer machine 63 to cool the chiller. The circulation tube 30 leading to the freezing machine 63 is connected to the freezing machine or to a turbine generator to generate the electricity, using the hot water or steam circulating in the circulation tube 30. In addition, this tube can be used to operate the burner, the fan, the drying oven, the dry plates, the grate plates, the freezing machine used in the multifunction destruction apparatus 1, the opening / closing valve, or as a power supply for a belt conveyor for the entry of garbage or in an air cooler provided in the facilities. In addition, night electricity and incineration heat are used, and the freezing machine is also used. Ice storage is used for an air cooler in the facility. Of course, the generator is not restricted to the turbine generator, and can be used together with a wind turbine, a photovoltaic generator, a liquid hydrogen generator, a fossil fuel from a solar battery, an accumulator battery and other generators, instead of the turbine generator. In addition, a method of generating energy that uses no atomic energy can be adopted. A circulation tube 64 for circulating the cooling water for an air cooler in the facilities, or a quarter using the thermal heat of the water tank 59 is inserted into the water tank 59 of the cooling tank portion 9. A opening / closing degree of the opening / closing valve 59b of the water tank 59, and the opening / closing valve 61b of the cooling tube 61 of the cooling tank portion 9 and the operation of the freezing machine 63 can be automatically controlled by a computer. Sensors may be provided to detect a temperature, a moisture content, a water level, a vacuum condition and other measurements in the water tank 59, the air cooling tube 61 and other components, to enable automatic control by a computer. Figure 6 is a general cross-sectional view illustrating one embodiment of the multifunctional destruction apparatus according to the present invention. In this embodiment, the heat radiators 68 connected to the heat pipe 67 are replaced by the heating burners 20a, 43b and 55 installed in the dry combustion furnace 2, the smoke combustion portion 5, and the air heating portion. 8 of the multifunctional destruction apparatus 1 illustrated in Figure 1. The heat pipe 67 transmits the heat of the solar energy collected by a parabolic condenser 66 placed outside the multifunctional destruction apparatus to the heat radiators 68 provided for the cameras 20, 42e and 57 of the dry combustion furnace 2, the smoke combustion portion 5 and the air heating portion 8. One end of the heat pipe 67 is connected to the parabola condenser 66, and branching the heat pipes 67a, 67b and 67c. In addition, the other ends of the heat pipes 67a, 67b and 67c are connected to the heat radiators 68 to transmit the heat of the condenser 66. As with the material of the heat pipes 67a, 67b and 67c, the pipes that They use a heat transfer metal and its material or tubes that use ceramics as their material can be used. The structure can be adopted to transmit the heat of the solar energy to the respective heat radiators 68, using the parabola capacitor 66 as a lens condenser. Alternatively, a method can be used to convert the energy into electricity to transmit the heater's heat. In the multifunctional destruction apparatus the one illustrated in Figure 6, although the first smoke feed portion 4 and the dust filter portion 6 provided with the multifunction destruction apparatus 1, illustrated in Figure 1 are not shown, the first The smoke feed portion 4 and the dust filter portion 6 may or may not be supplied. The dry combustion furnace 2 of the multifunctional destruction apparatus, is provided with an ash access door 18a for the purpose of removing the incinerated ash accumulated in the ash tray 17c to the exterior of the dry combustion furnace 2, but the rails d are provided inside or outside the access door of the ash. ash 18a and wheels and the like can be adhered to the ash tray 17c to make it possible to slide, in order to facilitate access to the ash tray 17c. In addition, a worm conveyor or belt conveyor can be attached, instead of the rails 17d. In the dry combustion furnace 2 of the multifunctional processing apparatus la, the funnel ventilation access door 24 is provided in order to remove the funnel ventilation accumulated in the funnel ventilation tray 23 to the outside of the dry combustion furnace 2, but the rails 23a are provided inside or outside the access door of the funnel vent 24, and wheels and the like are also adhered to the funnel ventilation tray 23 to make possible their sliding in order to provide access to the funnel ventilation tray 23. In addition, an auger conveyor or belt conveyor can be attached instead of the rails 23a. A vibrating belt conveyor can also be used. In addition, a screw conveyor 65 is provided in order that the ash access door 18a is open to remove the ash pan 17c and the ash accumulated in the ash pan 17c is moved to the drying furnace 3. The belt conveyor, or vibrating belt conveyor and the like can be employed as a screw conveyor 65. Of course, the operation of the opening / closing valve, the burner, the fan, the conveyor, the parabolic condenser and similar components provided for the multifunctional destruction apparatus illustrated in Figure 6 can be automatically controlled by a computer. Sensors can be provided to detect a temperature, a humidity, a water level, a vacuum condition and other measurements to enable automatic control by a computer. Figure 7 is a partially enlarged view of another embodiment of the multifunctional destruction apparatus according to the present invention. In this embodiment, the first smoke feed portion 4 provided at the rear of the drying oven 3 of the multi-functional destruction apparatus 1 and the one provided is in the form of an ash casting portion 71 and a smoke feeding portion. 77. The structure in which the ash casting portion 71 and the smoke feed portion 77 are located in the rear part of the dry combustion furnace 2 can also be adopted. A gas conduit 70 is provided which extends from the center of one end 31b of the drying oven 3 in the drying oven 3, and the ash casting portion 71, and the gas conduit 75 and the smoke feed portion 77 are continuously provided to the other end of the gas channel 70. The ash casting portion 71 is constituted by a melting furnace 72 having a cover 72a, a heating burner 73, a crucible 74 having a cover 74a, and a refractory brick 74b. The cover 72a is adhered to the upper face of the melting furnace 72 having a refractory impeller and a similar one on the surface of the inner wall thereof, so that the cover can be opened / closed, and the heating burner 73 oriented diagonally upwards is placed on the lateral surface thereof. The refractory bricks 74b are heated in the interior bottom of the melting furnace 72, or the refractory impeller is used to build a base and the crucible 74 is mounted and formed therein. The crucible 74 has a cylindrical shape, and a plurality of leg portions extending outwardly from the bottom face while the top face is open. The cover 74a has a hole that is placed on the upper face, and the incinerated ash obtained from the dry combustion furnace 2 or the drying oven 3, is accommodated in the crucible 74. The hot air containing the smoke supplied from the drying oven 3, or the dry combustion furnace 2 is used to completely burn a small amount of the remaining unburnt gas, funnel ventilation, toxic gases such as COx, SOx, NOx and other gases, dioxins at a temperature of approximately 1300 ° C to 1800 ° C by the heating burner relatively large 73 provided with the ash melting furnace 71. The crucible 74 can be heated by the high heat obtained by heating the heating burner 73, and the incinerated ash accommodated in the crucible 74 can be melted. The flame surrounding the crucible 74 has a spiral shape around the crucible 74 due to the hot air coming from the drying oven 3, or the dry combustion furnace 2, the combustion energy of the mixed gas and the provision of the heating burner 73 in an orthogonal lower portion, thereby heating the entire crucible 74 in a uniform manner. When refractory bricks 74b are provided around the crucible 74, the interior of the ash melting furnace 72 can be maintained at a high temperature by the heat storage and the heat retention effect. If a space is provided around the crucible 74 for filling the refractory bricks 74b or the refractory impeller and the like therein, the interior of the crucible 74 can be further stabilized at a high temperature. The incinerated ash obtained by the incineration of paper or wood, raw waste, resin and other objects, which can be included in the incinerated regular ash, can be used to finish the carbonization by combustion, as well as the evaporation of the carbon components. , oxygen, nitrogen and others, at extremely high temperatures. However, a small amount of non-combustible materials such as metals, heavy metals, glass and other materials are usually mixed in any other component of the combustible object to be incinerated. Heavy metal is contained in incinerated ash, and can adversely affect animals and humans or nature, when incinerated ash is used as landfill, as it is. Therefore, the incinerated ash can be melted in an ash melting furnace 72 and cooled to be hardened for destruction. Subsequently, the cover 72a is opened to remove the cover 74a, and the agglomerate in the crucible 74 is taken out and cooled to be hardened. The agglomerate obtained by the casting and hardening of the ash, is a transparent agglomerate similar to a marble that contains heavy metals and other materials. The molten object thus obtained from the incinerated ashes, can be destroyed by being mixed in cement or the like for the formation of gravel from an aggregate for a construction material or concrete. A filter 76 is provided in the gas conduit 75 which connects the ash cast portion 71 to the smoke feed portion 77. The dust collection / filtration effect of the filter 76 is increased using a thermal catalytic filter, a filter of ceramics and others. The obstruction of the filter can be suppressed, since the complete incineration is carried out using the combustion heat in the frontal stage. The lumps can be burned when a burner and similar equipment is attached. Any type of filter 76 that filters air, steam and others through it can be used. The 50 angstrom to 500 angstrom pores are produced for the filter, and the interior of the dry combustion chamber 2 and the filter of the drying oven 3 form a vacuum when the air molecules pass through the pores. When the filter 76 is used as a ceramic filter and pores form 50 angstroms to 500 angstroms, smoke molecules and the like do not pass through the pores. It should be noted that a ceramic filter can not be used, since the number of molecules in the air is several angstroms per 50 angstroms. The smoke feed portion 77 is constituted by a centrifugal furnace 78 having a cover 78a, a burner 79, a fan 80, an air supply tube 80a and a gas conduit 81. As a tip of the supply pipe of air 80a adhered to the fan 80 is inserted slightly into the end of the pipe 81a of the gas conduit 81, the air supplied from the tip 80b of the air supply pipe 80a connected to the fan 80, is blown to the lower end 81a of the air channel gas 81. The air is further expelled to the gas conduit 81 while the smoke, hot air and the like are admitted in the centrifugal furnace 78, by the effect of the expeller, and the interior of the centrifugal furnace 78 constantly forms a vacuum. Hot air, smoke and others, blown from the ash casting portion 71 are blown from the upper portion of the centrifugal furnace 78 and gradually move down the funnel vent contained in the hot air or smoke while rotating in the air. the centrifugal furnace 78. At this point, when the burner 79 is adhered to accelerate the direction of rotation of the hot air or the smoke used to burn again the hot air, the smoke and other emissions, these are burned completely so as not to be toxic . A vortex flow in the centrifugal furnace 78 causes the flame of the burner 79 to extend extremely long, and the hot air or smoke comes into contact with the flame for a long period of time, thereby maintaining the interior of the flame. Centrifugal oven 78 at a high temperature. A crucible 82 is provided to melt and harden the ash on the outer peripheral surface of the gas conduit 81, formed in the center of the centrifugal furnace 78. As illustrated in Figure 7, the crucible 82 is constituted by a double cylinder and has a structure in which a bottom is formed between the outer cylinder and the inner cylinder. In addition, a cover 82a having a hole in the upper face is placed. In this way, the results of melting, heat radiation, and heat storage can be obtained simultaneously. The flame of the burner having a spiral shape, keeps the crucible 82 at a high temperature and melts the ash accommodated in the crucible 82. After opening the cover 78a of the crucible 82 and removing the cover 82a, the molten object is cooled and hardened after removing it from the crucible. The air supplied from the air supply tube 80a from the fan 80 can cool the hot air in the centrifugal furnace 78 to a high temperature in a blast, and supply the air in the centrifugal furnace 78 for the gas conduit 81. therefore, toxic substances, such as dioxins, NOx, SOx, HCl and others contained in hot air or smoke, can be pyrolyzed in the centrifugal furnace 35 to remove smoke, dust and other components. The operation of the burner 79, the fan 80 provided for the smoke feed portion 77 can be automatically controlled by a computer. Sensors can be provided to detect a combustion temperature, an exhaust temperature, a water content, a vacuum condition and others in the centrifugal furnace 78 in order to make automatic control possible. Referring to Figures 8 to 16, a method is provided for the destruction of an object to be destroyed using the multifunctional destruction apparatuses 1 and the one according to the present invention, which will be described in detail to continuation. That is, a description will be provided regarding the method for the destruction of raw waste, sediment, general waste, expanded polystyrene, polymer-based substances and other objects, using the multifunctional destruction apparatus 1 illustrated in Figures 1 to 5, the multifunctional destruction apparatus illustrated in Figure 6, the cast iron portion and the feed portion of smoke illustrated in Figure 7 and the processing steps thereof. Figure 8 illustrates a method of destruction by microbial degradation; Figure 9, a method of destruction by pyrolysis; Figure 10, a method of destruction by drying at low temperature; Figure 11, a destruction method by indirect hot air drying; Figure 12, a destruction method by direct drying by hot air; Figure 13, a method of destruction by carbonization; Figure 14, a destruction method by incineration; and Figure 15, a method of shattering expanded polystyrene and polymer-based substances. Here, there are two methods of indirect hot air drying. Figure 8 is a flow chart illustrating a method of destruction by application of microbial degradation to the raw waste or sediment, using the multifunctional destruction apparatus. The destruction method of this example maintains raw refuse, sediment and the like at an appropriate temperature to be fermented or decomposed using microbes or fungi.

"Introduction of Raw Waste / Sediment - Process 101" Raw waste or sediment is introduced into the first dry chamber 15 through the inlet opening 13a of the raw waste / sediment input portion 13 provided for the dry combustion furnace 2 of the multifunctional destruction apparatus 1 or the one, illustrated in Figure 2 or Figure 6. The dry plate 15a, and the respective grid plates 15c, 15e and 15g, are rotated so that the raw waste or sediment can be accommodated evenly in the respective dry chambers 15, 15b, 15d and 15f. When the sediment to be introduced is an active sediment, which can be obtained by the decomposition process by the active sediment method, the microbial degradation advances a little later. Of course, the raw refuse or sediment can be introduced through the doors 16 and 16a of the dry combustion furnace 2 into the respective dry chambers 15, 15d and 15f, or the raw waste or the sediment can be introduced by the opening of the entrance of the general refuse inlet portion 14 or the door 18 into the combustion chamber 17. This is because in this method of destruction, the incineration by combustion is not carried out in the combustion chamber. combustion 17. Raw refuse or sediment may be introduced through the inlet opening 32a of the garbage inlet portion 32 provided in the drying oven 3 illustrated in Figure 3, Figure 6 or Figure 7 within the drying oven 3 This is because in this method of destruction, destruction by dry incineration in the drying oven is not carried out.

"Heating Process 102" The heating burner 20a provided for the bottom of the dry incinerator 2 illustrated in Figures 2 and 3 is turned on, or the heat radiator 68 shown in Figure 6 is operated. At the same time, the opening / closing valve 58a of the air supply tube 58 of the air heating portion 8 shown in Figures 3, 5 or 6 is closed, and the opening / closing valve 61b of the cooling tube of air 61 of the portion of the cooling tank 9 and the opening / closing valve 22a of the air supply pipe 22 of the dry combustion furnace 2 are opened. The fresh air is admitted from the air cooling tube 61 to be led from the air supply tube 22 to the dry combustion furnace 2. The cooling tank portion 9 may or may not be operated. The fresh air admitted to the dry combustion furnace 2 is heated by the heat of a heating burner 20a radiated from a heat radiator tube 20b. The hot air, which passes into the heat radiator tube 20b and is obtained by the heating burner 20a, passes through the exhaust pipe 21 to be expelled to the air intake box Ia after the heat radiation.

"Suction - Step 103" The fan 39 of the first smoke feed portion 4 or the fan 52 of the second smoke feed portion 7 shown in Figures 3, 5 or 6 is operated, or the fan 80 of the portion Smoke feed 77, illustrated in Figure 7, is operated so that the interior of the dry combustion furnace 2 and that of the drying oven 3 form a low vacuum condition. Any or some of the respective fans 39, 52 and 80, or all of them, can be operated. When the fans 39, 52 and 80 are operated, the control is executed in such a way that the interior of the ovens 2 and 3 completely form a low vacuum condition. By forming a low vacuum condition in the dry combustion furnace 2, the fresh air driven to the dry combustion furnace 2 to be heated, passes slowly through the respective dry chambers 15, 15b, 15d and 15f, and the combustion chamber 17 while the circulation is repeated. In addition, this fresh air heats the raw waste or the sediment accommodated in the same chambers 15, 15b, 15d, 15f and 17. The hot air that has passed through the combustion furnace 2 is led to the drying oven 3 by means of the pipe smoke conductor 29 for heating the raw waste or the sediments accommodated in the drying oven 3. The fermentation is carried out by causing the drying oven 3 to rotate the cylindrical body 31.

"Degradation by Fermentation by Heat Retention Step 104" The raw waste, and the sediments accommodated in the respective dry chambers 15, 15b, 15d and 15f and the combustion chamber 17, are kept warm at a temperature suitable for the microbes and fungi that exist in the raw waste or sediments, are activated by the proper continuous operation of the heating burner 20a of the combustion furnace 2 and also continuously operating the fans 39, 52 and 80 in a suitable manner. The microbes or fungi are cultivated to ferment or degrade raw waste or sediment. Of course, Microbes or fungi for advanced fermentation / degradation can be placed in the respective dry chambers 15, 15b, 15d and 15 and in the combustion chamber 17. When the vacuum condition is formed to absorb the air by ventilation, the air can be taken in a balanced way with respect to raw waste, sediment and other objects, which are the object to be incinerated, thus accelerating the fermentation / degradation.

"Deodorization - Step 105" The odor of the fermentation, and the odor of the degradation are subjected to the combustion process by operating the burner 37 of the first smoke feed portion 4 and the burner 50 of the second smoke feed portion 7 or the combustion portion 5 illustrated in Figures 3, 4, 5 or 6 or by operating the burner 79 of the smoke feed portion 77 illustrated in Figure 7. The deodorized gas is expelled from the conduit 53 of the second portion of smoke feed 7 outside the multifunctional destruction apparatus 1 or la. At this point, the dust filter apparatus 46 of the dust filter portion 6 is not used. The opening / closing valve 44a of the gas conduit 44 is closed, and the opening / closing valve 45a of the gas conduit is closed. 45 is open, so that the gas to be expelled is diverted from the smoke combustion chamber 5 to the second smoke feed portion 7.

"Collection of Objects for Destruction - Step 106" The object to be destroyed, such as the raw garbage or the sediments accommodated in the dry combustion furnace 2 can be removed from the doors 16, 16a and 18 at the end of the fermentation / degradation using microbes or bacteria. The objects to be destroyed, such as the raw garbage or the sediments accommodated in the drying oven 3 can be collected in the storage chamber 33 to be accommodated or collected.

The objects for destruction removed from the doors 16, 16a, and 18 or the storage chamber 33 can be processed in any other step of the process, and the object to be destroyed obtained from the raw waste, or the sediment can be used, for Of course, as fertilizers, for a sowing plot or a fruit farm, a kitchen garden, a wadi and others, or food products for domestic animals, such as pigs. In addition, they can be accommodated in the dry combustion furnace 2 and incinerated as trash that can be burned later. Figure 9 is a flow chart illustrating a method for pyrolyzing general refuse, or incinerated ash, using the multifunctional destruction apparatus in accordance with the present invention. The method of destruction in this example pyrolyses hazardous substances, such as hazardous gases, for example, COx, SOx, and dioxins contained in general waste, or incinerated ash and the like, including raw waste or sediments at an extremely high temperature high so that it is not toxic.

"Trash Introduction Process 111". Raw refuse or sediments are introduced from the raw waste / sediment input portion 13 provided in the dry combustion furnace 2 of the multifunctional destruction apparatus 1 or that of Fig. 2 or Fig. 6 into the first dry chamber 15, and general waste or ash incinerated, are introduced from the inlet opening 14a of the general refuse input portion 14. The incinerated ash can be introduced from the doors 6, 6a and 18 into the respective dry chambers 15, 15d and 15f or the combustion chamber 17 , or the remaining incinerated ash in the ash tray 17c can be left as is, because it can be degraded. In addition, the raw refuse or sediment can be accommodated in a balanced manner in the respective dry chamber 15, 15b, 15d and 15f by rotating the dry plate 15a and the respective grid plates 15c, 15e and 15g.

"Heating Process 112". The heating burner 20a provided for the lower portion of the dry incinerator 2 illustrated in Figures 2 and 3 is turned on, or the heating radiator 68 shown in Figure 6 is operated. At the same time, the opening / closing valve 58a of the air supply tube 58 of the air heating portion 8 shown in Figure 3, Figure 5 or Figure 6 is closed, and the opening / closing valve 61b of the tube of air cooling 61 of the cooling tank portion 9 and the opening / closing valve 22a of the air supply pipe 22 of the dry combustion furnace 2 are opened. The fresh air is taken from the air cooling tube 61 to be conducted from the air supply tube 22 into the dry combustion furnace 2. The cooling tank portion 9 may or may not be operated. The admitted fresh air from the dry combustion furnace 2 is heated by the heat from the heating burner 20a, radiated from the heat radiator tube 20b. the dry air obtained by the heating burner 20a passing through the heat radiator tube 20b is radiated and then passed through the exhaust pipe 21 to be emitted into the air intake box lia.

"Suction - Step 113". The fan 39 of the first smoke feed portion 4 or the fan 52 of the second smoke feed portion 7 illustrated in Figure 3, 5 or 6 are operated, or the fan 80 of the smoke feed portion 77 illustrated in Figure 7 it is operated, so that the interior of the dry combustion furnace 2 and the interior of the drying oven 3 form a vacuum. Any of them or any of the respective fans 39, 52 and 80 can be operated or all of them can be operated. When the inside of the combustion furnace dries 2 forms a vacuum, the fresh air conducted inside the dry combustion furnace 2 to be heated passes through the respective dry chambers 15, 15b, 15d and 15f and the combustion chamber 17 and heats the raw waste, or the settled sediment in the dry chamber 15, 15b, 15d and 15f and the general refuse or incinerated ashes accommodated in the combustion chamber 17. At this time, the dust filter apparatus 46 of the dust filter pot 6 is not used. The opening / closing valve 44a of the gas conduit 44 is closed and the opening / closing valve 45a of the gas conduit 45 is opened, so that the gas to be expelled from the smoke combustion portion 5 is diverted to the second portion of smoke feed 7.

"Sealing Process 114". When the dry combustion furnace 2 is heated uniformly (at temperatures of about 300 ° C to 500 ° C) the operation of the respective fans 39, 52 and 80 is stopped. Also, the opening / closing valves 29a of the smoke guide tube 29 and the opening / closing valve 22a of the air supply tube 22 illustrated in Figures 2, 3, 5 or 6 are closed, so that the interior of the dry combustion furnace 2, for example, the respective dry chambers 15, 15b, 15d and 15f and the combustion chamber 17 are completely sealed.

"Pyrolysis Process 115" When completely sealed, the interior of the dry combustion furnace 2, contains a large amount of unburned gas and unburnt carbon generated at a high temperature, and lacks oxygen to be in the reduced atmosphere. Under the reduced atmosphere, hazardous substances, such as carbon monoxide and dioxins, can be prevented and the density of oxygen is extremely thin under the reduced atmosphere. When additional heating is applied, and pyrolyzing at a temperature of not less than 450 ° C, the dioxins become non-toxic, and the nitrogen oxide, a sulfur oxide and a hydrogen chloride are pyrolyzed, thereby reducing a amount of hazardous substances, such as dioxins, NOx, SOx HCl and others, contained in the gas generated due to pyrolysis.

"Process of Collection of Objects for Destruction 116". The object for destruction such as general waste, an incinerated ash containing raw waste and a sediment accommodated in the dry combustion furnace 2 can be removed through the doors 16, 16a and 18 after pyrolysis under reduced atmosphere. The object for destruction taken from the doors 16, 16a and 18 can be processed in any other processing step, and the destruction object obtained from the raw waste or sediment can be used, of course, as fertilizer, for a plot of land. sowing or a fruit farm, or a kitchen garden, dry streams and others, or food products for pets, such as pigs. It can also be accommodated in the dry combustion furnace 2, and later incinerated as garbage that can be burned. Figure 10 is a flow chart illustrating the method for applying the low temperature drying process to the raw waste or sediment, using the multifunctional destruction apparatus according to the present invention, illustrated in Figure 10. The method of destruction of this example, dry the raw waste and / or the sediment at a low temperature without generating odor.

"Operation of the Cooling Tank Port - Step 121" Water, rainwater or other liquids are first introduced into the water tank 29 of the ep-frying air portion 9 illustrated in Figure 4, from the opening of the tank. inlet 59a provided for water tank 59, and water is stored while regulating the inlet using an opening / closing valve 59b. in an area of heavy snowfall, snow, ice and others can be stored, and snow, ice and other stored, can be introduced from the opening of entry 59a. Using night energy, or using the energy obtained from a wind power generation, turbine power generation, a generation of solar energy, and other systems, the freezer machine 63 is operated to produce a frozen ice 62a in the tank of water 59 by the endothermic tube 62. The cooling of the interior of the water tank 59 causes the fresh air passing through the air guide tube 60 and the air cooling tube 61 to be cooled and dried. In particular, cool dry cold air passing through the air cooling tube 61 is conducted inside the dry combustion furnace 2 via the air supply tube 22. When the freezing machine is operated using the night energy to use the Thermal storage of the ice, the cold blast can be used during the day.

"Trash Introduction - Step 122". The raw refuse or sediment is introduced into the first dry chamber 15 from the inlet opening 13a of the raw waste / sediment input portion 13 provided in the dry combustion furnace 2, of the multifunctional destruction apparatus 1 or illustrated in Figure 2 or 6. The dry plate 15a, and the respective grid plates 15c, 15e and 15g, are rotated so that the raw refuse or sediment can be accommodated in a uniform manner in the dry chambers 15, 15b, 15d and 15f respectively. Raw refuse or sediment can be introduced from the doors 16 and 16a of the dry combustion furnace 2 into the respective dry chambers 15, 15d and 15f, or the raw garbage or the sediment, can be introduced from the inlet opening 14a of the general garbage inlet portion 14 or the door 18 of the combustion chamber 17. This is because the destruction by incineration by combustion is not performed in the combustion chamber 17 in this processing method. Raw refuse or sediment may be introduced into the drying oven 3 from the inlet opening 32a of the garbage inlet portion 32 provided in the drying oven 3 illustrated in Figures 3, 6 or 7. This is due to that destruction by dry combustion is not performed in the drying oven 3 in this processing method.

"Ventilation - Step 123". The opening / closing valve 58a of the air supply tube 58 of the air heating portion 8 illustrated in Figures 3, 5 or 6 is closed, and the opening / closing valve 61b of the air cooling tube 61 of the portion of the cooling tank 9 and the opening / closing valve 22a of the air supply pipe 22 of the dry combustion furnace 2 are opened. The dry cool cold air passing through the air cooling tube 61 is conducted into the dry combustion furnace 2 via the air supply tube 22. When the air is conducted inside the dry combustion furnace 2, the cold air fresh dry that passes through the air supply tube 22, is cooled to be at a temperature no greater than about 5 ° C in the cooling tank portion 9 and to be absorbed into the oven.

"Drying by Suction - Step 124" The fan 39 of the first smoke feed portion 4 or the fan 52 of the second smoke feed portion 7 illustrated in FIGS. 3, 5 or 6 is operated or the fan 80 of the The smoke feed portion 77 illustrated in Figure 7 is operated, so that the interior of the dry combustion furnace 2 or that of the drying oven 3 form a vacuum. Any or any of the respective fans 39, 52 and 80 can be operated, all can be operated. When the inside of the combustion furnace dries 2 forms a vacuum, cool dry cool air conducted inside the dry combustion furnace 2 passes slowly through the respective dry chambers 15, 15b, 15d and 15f and the combustion chamber 17 while the circulation is repeated and dried and cooled the raw refuse, or the sediment accommodated in the chambers 15, 15b, 15d, 15f and 17. The dry cold air that has passed through the dry combustion furnace 2 is conducted inside the drying oven 3 by means of the conductive tube of smoke 29 and dry and cool the raw refuse or sediment accommodated in the drying oven 3. The drying oven 3 rotates the cylindrical body 31 to continue drying.

"Deodorization - Step 125" The burner 37 of the first smoke feed portion 4, the burner 50 of the second smoke feed portion 7 or the smoke combustion portion 5 illustrated in Figures 3, 4, 5 or 6 is operated, or the burner 79 of the smoke feed portion 77 illustrated in Figure 7 is operated, so that the odor obtained from the interior of the dry combustion furnace 2 and that of the drying oven 3 is subjected to the combustion process . The deodorized gas is expelled from the conduit 53 of the second smoke feed portion 7 to the outside of the multifunctional destruction apparatus 1 or la. Here, the dust filter apparatus 46 of the dust filter portion 6 is not used. The opening / closing valve 44a of the gas conduit 44 is closed and the opening / closing valve 45a of the gas conduit 45 is opened, so that the gas to be expelled is diverted from the smoke conduction portion 5 to the second smoke feed portion 7. In the low temperature drying processing method of this example, because the odor is hardly generated, the burner 37 of the first smoke feed portion 4, the burner 50 of the second smoke feed portion 7, the smoke combustion portion 5 and the burner 79 of the smoke feed portion 77 may not to be operated, and the deodorization step 125 may be omitted.

"Collecting Objects for Destruction - Step 126". The object to be destroyed such as raw garbage or sediments accommodated in the dry combustion furnace 2 can be removed by the doors 16, 16a and 18 at the end of the drying process using the cold air. The object to be destroyed, such as raw garbage or the sediment accommodated in the drying oven 3 can be collected in the storage chamber 33 to be accommodated or collected. The object for destruction removed by the doors 16, 16a and 18 by the storage chamber 33 can be processed in any other step of the process, and the object for destruction obtained from the raw waste or sediments can be used, of course, as fertilizers of a cultivation land or a fruit farm, a kitchen garden or a wadi or others or for food products for pets, such as pigs. In addition, it can be accommodated in the dry combustion furnace 2 and later incinerated as garbage that can be burned. Figure 11 is a flow chart illustrating the method for drying general refuse, raw waste or hot air heated sediment using the multifunctional destruction apparatus according to the present invention. The method of destruction by indirect hot air drying, in this example, dries general waste, raw waste or sediment at an average temperature (approximately 40 ° C to 400 ° C) without generating odor.

"Trash Introduction Process 131" Raw waste or sediment is introduced into the first dry chamber 15 by the inlet opening 13a of the raw waste / sediment input portion 13 provided in the dry combustion furnace 2 of the waste apparatus. multifunctional destruction 1 or that illustrated in Figure 2 or 6, and general waste is introduced from the entry opening 14a of the general refuse input portion 14. The dry plate 15a and the respective grate plates 15c, 15e and 15g, they are rotated so that the raw refuse or sediment can be accommodated uniformly in the dry chambers 15, 15b, 15d and 15f, respectively.

Raw refuse or sediment can be introduced from the doors 16 and 16a of the dry combustion furnace 2 into the respective dry chambers 15, 15d and 15f, or the raw garbage or the sediment can be introduced from the inlet opening 14a of the general refuse input portion 14 or the door 18 within the combustion chamber 17. This is because the destruction by incineration by combustion is not performed in the combustion chamber 17 in this processing method. In addition, raw refuse or sediment may be introduced into the drying oven 3 from the inlet opening 32a of the garbage inlet portion 32 provided for the drying oven 3 illustrated in Figures 3, 6 or 7. That is because the destruction by dry combustion, is not performed in the drying oven 3 in this processing method.

"Heating - Step 132" The heating burner 20a provided in the lower portion of the dry incinerator 2 illustrated in Figures 2 and 3 is ignited, or the heat radiator 68 of the dry combustion furnace 2 illustrated in Figure 6 is operated. At the same time, the opening / closing valve 58a of the air supply tube 58 is opened and the opening / closing valve 61b of the air cooling tube 61 of the cooling tank portion 9 and the opening / closing valve 22a of the air supply tube 22 of the dry combustion furnace are opened. The heating burner 55 of the air heating portion 8 is not operated. The dry cool cold air is taken from the air cooling tube 61 and the air supply tube 58 to be led from the air supply tube 22 to the dry combustion furnace 2. The cooling portion of the tank 9 is operated and the air found in the air cooling tube 61 is cooled and dried as much as possible. The dry cool cold air taken into the dry combustion furnace 2 is heated by the heat of the heating burner 20a radiated from the heat radiator tube 20b, at a temperature of about 70 ° C to 400 ° C. The hot air obtained by the heating burner 20a passing through the heat radiator tube 20b is heated by radiation and then expelled to the air intake box a by means of the exhaust pipe 21. In addition, the heat radiator pipe It can have the shape similar to a tray of a fryer.

"Drying by Suction - Step 133 The fan 39 of the first smoke feed portion 4 or the fan 52 of the second smoke feed portion 7 illustrated in Figures 3, 5 or 6 is operated. The smoke feed portion 77 illustrated in Figure 7 is operated so that the interior of the dry combustion furnace 2 and that of the drying oven 3 form a vacuum, either or both of the respective fans 39, 52 and 80 can be operated or all can be operated.When the interior of the dryer combustion furnace forms a vacuum, the dry cool cold air conducted inside the dry combustion furnace 2 passes slowly through the respective dry chambers 15, 15b, 15d and 15f, and the combustion chamber 17 while the circulation is repeated and dry and cool the general garbage, the raw garbage or the sediment accommodated in these chambers, 15, 15b, 15d, 15f and 17. The dry cold air that has passed through the furnace of combu The dry stucture 2 is led into the drying oven 3 by means of the smoke pipe 29 for drying and cooling the raw waste or the settled sediment in the drying oven 3. The drying oven 3 rotates the cylindrical body 31 to make drying.

"Deodorization - Step 134" The burner 37 of the first smoke feed portion 4, the burner 50 of the second smoke feed portion 7 or the smoke combustion portion 5 illustrated in Figures 3, 4, 5 or 6 it is operated. Or the burner 79 of the smoke feed portion 77 illustrated in Figure 7 is operated, so that the odor obtained from the interior of the dry combustion furnace 2 and that of the drying oven 3 is subjected to the combustion process. The deodorized gas is expelled from the conduit 53 of the second smoke feed portion 7 to the outside of the multifunctional destruction apparatus 1 or la. Here, the dust filter apparatus 46 of the dust filter portion 6 is not used. The opening / closing valve 44a of the gas conduit 44 is closed and the opening / closing valve 45a of the gas conduit 45 is opened , so that the gas to be expelled is diverted from the smoke combustion portion 5 to the second smoke feed portion 7. As it is difficult to generate odor, in the indirect hot air drying process method of this example, the deodorization step 134 can be omitted without operating the burner 37 of the first smoke feed portion 4, the burner 50 of the second smoke feed portion 7, the smoke combustion portion 5 and the burner 79 of the smoke feed portion 77.

"Object Collection Process for Destruction 135" The object to be destroyed such as general garbage, raw garbage or sediment can be removed through the doors 16, 16a and 18 at the end of the drying process using dry hot air. The raw refuse, or the sediment accommodated in the drying oven 3 can be collected in the storage chamber 33 to be accommodated or collected. The object for destruction is removed by the doors 16, 16a and 18 or the storage chamber 33 can be processed in any other step of the process, and the destruction object obtained from the raw waste or the sediment can be used, of course, as fertilizers for a farm land or a fruit farm, or a kitchen garden, wadi and others or for food products for domestic animals, such as pigs. It can also be accommodated in the combustion furnace and subsequently incinerated as garbage that can be burned. Although the indirect hot air drying process method of this example is advantageous because the dry chamber is not odorized with the combustion gas because the air heating portion 8 is not operated, the heat efficiency is low and only an average temperature (approximately 70 ° C to 400 ° C) can be obtained. Therefore, it is necessary to select the general garbage, the raw garbage or the sediment that is going to be dried, which does not contain heavy metals or toxic substances, that can be reused and reintroduced into the dry combustion furnace. or the drying oven 3. Figure 12 is a flow chart illustrating the method for drying general refuse, raw waste or hot air sediment using the multifunctional destruction apparatus according to the present invention. The hot air direct drying process method of this example dries general waste, raw waste or sediments at a high temperature (from about 400 ° C to 700 ° C) without the generation of odor.

"Garbage Introduction Process 141". The raw refuse or sediment is introduced into the first dry chamber 15 from the inlet opening 13a of the raw waste input portion 13 provided in the dry combustion furnace 2 of the multifunction destruction apparatus 1 or that illustrated in Figure 2 or 6, and the general garbage is introduced from the entry opening 14a of the general refuse input portion 14. The dry plate 15a and the respective grate plates 15c 15e and 15, are rotated so that the garbage or the sediment can be accommodated evenly in dry chambers 15, 15b, 15d and 15f respectively. Raw refuse or sediment may be introduced from the doors 16 and 16a of the dry combustion furnace 2 into the respective dry chambers 15, 15d and 15f, and the raw garbage or sediment may be introduced from the entry opening 14a of the the general refuse input portion 14 or the door 18 inside the combustion chamber 17. This is because in this processing method, destruction by incineration by combustion is not carried out in the combustion chamber. Additionally, raw refuse or sediment may be introduced into the drying oven 3 from the inlet opening 32a of the garbage inlet portion 32 provided for the drying oven 3 illustrated in Figures 3, 6 or 7. This is because the destruction by dry combustion is not carried out in the drying oven 3 in this processing method.

"Heating - Step 142" The heating burner 55 of the air drying portion 8 illustrated in Figure 5 is turned on, or the heat radiator 68 of the air drying portion 8 illustrated in Figure 6 is operated. At the same time, the opening / closing valve 58a of the supply tube 58 is opened, and the opening / closing valve 61b of the air cooling tube 61 of the cooling tank portion 9 and the opening / closing valve 22a of the air supply tube 22 of the dry combustion furnace 2 are closed. The heating burner 22a of the dry combustion furnace 2 is not operated. The fresh air is taken from the air tube 56 and the fresh air is heated by the heating burner 55 in the heating chamber 57. The heated air is converted into hot air which is to be conducted inside the dry combustion furnace 2 through of the air supply tube 58 and the air supply tube 22. The hot air conducted inside the dry combustion furnace 2 is heated to a high temperature of about 400 ° C to 700 ° C when it is conducted inside the combustion furnace dry 2"Drying by Suction - Step 143" The fan 39 of the first smoke feed portion 4 or the fan 52 of the second smoke feed portion 7 illustrated in FIGS. 3 and 6 is operated, or the fan 80 of FIG. the smoke feed portion 77 illustrated in Figure 7 is operated, so that the interior of the dry combustion furnace 2 and that of the drying oven 3 form a vacuum. Any of the respective fans 39, 52 and 80 can be operated, or all can be operated at the same time. When the interior of the dry combustion furnace 2 forms a vacuum, the hot air conducted inside the dry combustion furnace 2 passes slowly through the respective dry chambers 15, 15b, 15d and 15f and the combustion chamber 17, while the combustion chamber is repeated. circulation and drying with general hot air the general garbage, the raw garbage or the sediments accommodated in these chambers 15, 15b, 15d and 15f and 17. In addition, the hot air that has passed through the dry combustion furnace 2 is conducted inside of the drying oven 3 by the smoke guide pipe 29 for drying with hot air the raw refuse or the sediment accommodated in the drying oven 3. The drying oven 3 rotates the cylindrical body 31 to carry out drying.

"Deodorization - Step 144" The burner 37 of the first smoke feed portion 4 or the burner 50 of the second smoke feed portion 7 or the smoke combustion portion 5 illustrated in Figures 3, 4, 5 or 6 is operated, or the burner 79 of the smoke feed portion 77 illustrated in Figure 7 is operated so that the odor obtained from the interior of the dry combustion furnace 2, and the drying oven 3 is subjected to the combustion process. The deodorized gas is expelled from the conduit 53 of the second smoke feed portion 7 to the outside of the multifunctional destruction apparatus 1 or la. Here, the dust filter apparatus 46 of the dust filter portion 6 is not used. The opening / closing valve 44a of the gas conduit 44 is closed and the opening / closing valve 45a of the gas conduit 45 is opened , so that the gas to be expelled is diverted from the smoke combustion portion 5 to the second smoke feed portion 7. Because the odor is hardly generated in the direct hot air drying process method of this example, the deodorization step 134 can be omitted, without operating the burner 37 of the first smoke feed portion 4, the burner 50 of the second smoke feed portion 7, the smoke combustion portion 5 and the burner 79 of the smoke feed portion 77.

"Collection of Objects for Destruction - Step 145" The object for destruction such as general refuse, raw refuse or sediment accommodated in the dry combustion furnace 2 may be removed by the doors 16, 16a and 18 at the end of the drying process using hot air drying. The object to be destroyed, such as raw garbage or sediment accommodated in the drying oven 3, can be collected within the storage chamber 33 to be accommodated or collected. The object to be destroyed removed from the doors 16, 16a and 18 or the storage chamber 33 can be processed at any other processing step or it can be accommodated in the dry combustion furnace 2 as it is and subsequently be incinerated as a garbage that can burn. In the direct hot air drying processing method of this example, the dry air is smelled with the flue gas, because the air heating portion 8 is operated, but the heat efficiency is high and can be obtained a high temperature (from about 200 ° C to 500 ° C). Therefore, general waste, raw waste or sediment can be completely dried with air that has an extremely high temperature. Figure 13 is a flow diagram illustrating the method for the charring of general refuse, raw refuse or sediment, under a reduced atmosphere using the multifunctional destruction apparatus according to the present invention. In the processing method of this example, general waste, raw waste or sediment is burned and incinerated until it is completely charred while a minimum amount of oxygen is supplied.

"Trash Introduction - Step 151" Raw waste or sediment is introduced into the first dry chamber 15 from the inlet opening 13a of the raw waste / sediment input portion 13 provided for the dry combustion furnace 2 of the waste apparatus. multifunctional destruction 1 or the, and the general garbage is introduced from the entrance opening 14a of the general garbage inlet portion 14. The dry plate 15a and the respective grid plates 15c, 15e and 15g, are rotated so that the Raw refuse or sediment can be accommodated uniformly in the respective dry chambers 15, 15b, 15d and 15f. General waste, raw waste or sediment may be introduced into the drying oven 3 from the inlet opening 32a of the garbage inlet portion 32 provided in the drying oven 3 illustrated in Figure 3, 6 or 7.

"Heating - Step 152" The heating burner 55 of the air drying portion 8 illustrated in Figure 5 is turned on, or the heat radiator 68 of the air drying portion 8 illustrated in Figure 6 is operated. At the same time, the opening / closing valve 58a of the air supply tube 58 is opened, and the opening / closing valve 61b of the air cooling tube 61 of the cooling tank portion 9 and the opening valve / Closing 22a of the air supply tube 22 of the dry combustion furnace 2 are closed. The fresh air is admitted from the air tube 56, and the fresh air is heated by the heating burner 55 in the heating chamber 57. The heated air is converted into hot air to be conducted inside the dry combustion furnace 2, by the air supply tube 58 and the air supply tube 22. The hot air conducted inside the dry combustion furnace 2 is heated to an extremely high temperature and hardly contains oxygen, due to the heating burner 55. The burner heating 20a provided for the lower portion of the dry incinerator 2 illustrated in Figures 2 and 3 is ignited, or the heat radiator 68 illustrated in Figure 6 is operated. The hot air having an extremely high temperature admitted into the dry combustion furnace 2 is heated by heating the heating burner 20a radiated from the heat radiator tube 20b. The hot air obtained by the heating burner 20a, which passes through the heat radiator tube 20b is expelled inside the air intake box Ia, by the exhaust pipe 21 after the heat radiation. Also, the heat radiator tube may have the shape similar to a tray of a fryer.

"Smoke Combustion - Step 153" The burner 37 of the first smoke portion 4, the burner 50 of the second smoke feed portion 7 or the smoke combustion 5 illustrated in Figures 3, 4, 5 or 6 is operated , or the burner 79 of the smoke feed portion 77 illustrated in Figure 7 is operated so that the hazardous substances containing the odor and gas from the duct obtained from inside the dry combustion furnace 2 and from the furnace 3 drying, are subjected to the combustion process. The gas subjected to the gas combustion process is expelled from the conduit 53 of the second smoke feed portion 7 to the outside of the multifunctional destruction apparatus 1 or la. Here, it may or may not be used, the dust filter apparatus 46 of the dust filter portion 6. When the dust filter apparatus 46 is not used, the opening / closing valve 44a of the gas conduit 44 is closed , and the opening / closing valve 45a of the gas conduit 45 is opened, so that the gas to be expelled is diverted from the smoke combustion portion 5 to the second smoke feed portion 7.

"Suction Process 154" The fan 39 of the first smoke feed portion 4 or the fan 52 of the second smoke feed portion 7 illustrated in FIGS., 4, 5 or 6 is operated or the fan 80 of the smoke feed portion 77 illustrated in Figure 7 is operated, so that the interior of the dry combustion furnace 2, or that of the drying oven 3 forms a vacuum . Any or some of the respective fans 39, 59 and 80 can be operated or all of them can be operated. When the interior of the dry combustion furnace 2 forms a vacuum, the hot air conducted inside the dry combustion furnace 2 passes slowly through the respective dry chambers 15, 15b, 15d and 15f and the combustion chamber 17, while repeating the circulation and the general waste, the raw waste or the sediment accommodated in these chambers 15, 15b, 15d, 15f and 17 is dried with hot air. In addition, the hot air that has passed through the dry combustion furnace 2 is driven inside the drying oven 3 via the smoke pipe 29 for drying with hot air the raw refuse or the settled sediment in the drying oven 3. The drying oven 3 rotates the cylindrical body 31 for drying. By operating the fans 39, 52 and 80, an exhaust vortex flow and a flame formed in the centrifugal furnaces 35, 48 and 78 of the respective smoke feed portions 4, 7 and 77 are generated, so that the dangerous substances contained in the odor and gas of the duct, can be subjected to the combustion process.

"Carbonization - Step 155" The operation of the heating burner 55 of the air drying portion 8 illustrated in Figure 5 and the operation of the heat radiator 68 of the air drying portion 8 illustrated in Figure 6 continue, and the operation of the fan 39 of the first smoke feed portion 4 or the fan 52 of the second smoke feed portion 7 illustrated in Figures 3, 5 or 6 or the operation of the fan 80 of the smoke feed portion 77 illustrated in Figure 7 is continued. In addition, the operation of the heating burner 20a of the dry incinerator 2 illustrated in Figure 2 or 3 or the operation of the heat radiator 68 illustrated in Figure 6 continues, to maintain the interior of the dry combustion furnace 2 and that of the combustion furnace. 3 dried at an extremely high temperature. When the interior of the furnace is heated to a high temperature of approximately 300 ° C to 500 ° C where the general waste, raw waste or sediment is ignited or melted under reduced atmosphere, the opening / closing valve 22a of the air supply 22 of the dry combustion furnace 2 is completely closed, and the opening / closing valve 29a of the smoke pipe 29 is closed with a small opening. Then, the general garbage, the raw garbage or the sediment exposed to the hot air of high temperature, whose density of oxygen is thin from which the carbonization begins in a reduced atmosphere. Only the ejection is carried out by a vacuum, and said garbage is washed and baked in the respective dry chambers 15, 15b, 15d and 15f, the combustion chamber 17 and the drying oven 3. That is, the general garbage , raw waste or sediment is first dried with hot air having an average temperature of 300 ° C to 500 ° C, and subsequently, partially ignited in a small amount of admitted oxygen. The air is intercepted at the end of the admission of the general non-burned gases.

"Collecting Objects for Destruction - Step 156" The object for destruction such as general garbage, raw garbage or sediment which is accommodated in the dry combustion furnace 2 may be removed from doors 16, 16a and 18 after that the carbonization is over. The object for destruction, such as the raw garbage or the sediment accommodated in the drying oven 3 can be collected in the storage chamber 33 to be accommodated or collected. The object for destruction removed from the doors 16, 16a and 18 or the storage chamber 33 can be processed in any other step of the process or accommodated in the dry combustion furnace 2, since it will be destroyed by incineration later as garbage what can be burned Figure 14 is a flow diagram illustrating the method for the destruction of general refuse, raw waste or sediment by incineration in the reduced atmosphere, using the multifunctional destruction apparatus according to the present invention. The processing method of this example, destroys general waste, raw waste and sediment by combustion, without the generation of gases or hazardous substances.

"Trash Introduction - Step 161" Raw waste and sediment are introduced into the first dry chamber 15 by the inlet opening 13a of the raw waste / sediment input opening 13 provided in the dry combustion furnace 2 of the waste apparatus. multifunctional destruction 1 or that illustrated in Figures 2 or 6, and the general refuse is introduced by the entry opening 14a of the general refuse input portion 14. The dry plate 15a, the respective grate plates 15c, 15e and 15g, they are rotated so that the raw refuse or the sediment are uniformly accommodated in the respective dry chambers 15, 15b, 15d and 15f. In addition, general refuse, raw refuse or sediment may be introduced into the drying oven 3 through the inlet opening 32a of the garbage inlet portion 32 provided for the drying oven 3 illustrated in Figure 3, 6 or 7 "Heating - Step 162" The heating burner 55 of the air drying portion 8 illustrated in Figure 5 is turned on, or the heat radiator 68 of the air drying portion 8 illustrated in Figure 6 is operated. At the same time, the opening / closing valve 58a of the air supply tube 58 and the opening / closing valve 22a of the air supply tube 22 of the dry combustion furnace 2 are opened, and the opening / closing valve 61b of the air cooling tube 61 of the cooling tank portion 9 is closed. Fresh air is admitted from the air supply tube 56, and fresh air is heated by the heating burner 55 in the heating chamber 57. The heated air is converted to hot air to be conducted into the dry combustion furnace 2 through the air supply tube 58 and the air supply tube 22.

The heating burner 20a provided in the lower portion of the dry incinerator 2 illustrated in Figure 2 or 3 is ignited, or the heat radiator 68 shown in Figure 6 is operated. The hot air having an extremely high temperature, admitted into the dry combustion furnace 2 is heated by the heat from the heating burner 20a and radiated from the heat radiator tube 20b. The hot air obtained by the heating burner 20a which passes through the heat radiator tube 20a is heated by radiation to be then expelled to the air intake box lia through the exhaust pipe 21. In addition, the radiator pipe heat 20b can have the shape similar to a tray of a fryer.

"Smoke Combustion - Step 163" The burner 37 of the first smoke feed portion 4, the burner 50 of the second smoke feed portion 7 or the smoke combustion portion 5 illustrated in Figures 3, 4, 5 or 6 is operated, or the burner 79 of the smoke feed portion 77 illustrated in Figure 7, is operated so that the odor, gas from the duct, and the hazardous substances contained in the duct gas obtained from the interior of the dry combustion furnace 2 and the drying furnace 3 are destroyed by combustion. The gas subjected to the smoke combustion process is expelled from the conduit 53 of the second smoke feed portion 7 to the outside of the multifunctional destruction apparatus 1 or la. The smoke containing dangerous substances generated by the dry combustion furnace 2 is subjected to the catalytic combustion so that it is not toxic in the smoke combustion portion 5, to be supplied to the second smoke feed portion 7.

"Suction Filtration - Step 164" The fan 39 of the first smoke feed portion 4 or the fan 52 of the second smoke feed portion 7 illustrated in FIGS. 3, 5 or 6 is operated, or the fan 80 of FIG. the smoke feed portion 77 illustrated in Figure 7 is operated, so that the interior of the dry combustion furnace 2 and that of the drying oven 3 form a vacuum. Any or some of the respective fans 39, 52 and 80 can be operated, or all can be operated. In addition, since the regular combustion step is carried out in this processing method and the gases and hazardous substances contained in the smoke, the dust filter apparatus 46 of the dust filter portion 6 is used. dust filter apparatus 46, the opening / closing valve 44a of the gas conduit 44 is opened, the opening / closing valve 45a of the gas conduit 45 is closed, so that the gas expelled from the dry combustion furnace 2 and the drying oven 3 is conducted inside the dust filter apparatus 46. In the case of the processing of dioxins, a nitrogen oxide, a sulfur oxide, a hydrogen chloride, the funnel ventilation contained in the gas of the exhaust and exhaust, pass through the dust filter apparatus (a semiautomatic filter, an electric dust collector, a thermal catalyst, a calcium hydroxide, an activated carbon and others, a calcium oxide) 46, and the odor of the exhaust gas is so put into the combustion process by activating the burners 37 and 50 and the thermal catalyst apparatus 39.

"Combustion - Step 165" The general refuse, the raw waste or the sediment accommodated in the combustion chamber 17 of the dry combustion furnace 2 and the drying oven 3 are ignited. When the interior of the dry combustion furnace 2 forms a vacuum, the hot air conducted in the dry combustion furnace 2 passes slowly through the respective dry chambers 15, 15b, 15d and 15f and the combustion chamber 17, while repeating the circulation and burning of the general waste, the raw waste or the sediment accommodated in these chambers 15, 15b, 15d, 15f and 17. In addition, the hot air that has passed through the combustion furnace 2 is conducted inside the drying oven 3 by means of the smoke pipe 29 for burning the raw refuse or the settled sediment in the drying oven 3. The drying oven 3 rotates the cylindrical body 42 to effect dry combustion. The operation of the fans 39, 52 and 80 generates an exhaust vortex flow and an elongated flame in the centrifugal furnaces 35, 48 and 78 of the respective smoke feed portions 4, 7 and 77, so that the odor , the gas in the duct and the dangerous substances contained in the duct gas can be subjected to the combustion process.

"Process of Collection of the Object for Destruction 166" The object for destruction such as general refuse, raw refuse or sediment accommodated in the dry combustion furnace 2 can be removed by the doors 16, 16a and 18 at the end of the drying process using the dry hot air. The object for destruction such as raw garbage or sediment accommodated in the drying oven 3 can be gathered in the storage chamber 33 to be accommodated or collected. The object for destruction removed by the doors 16, 16a and 18 or the storage chamber 33 can be processed in any other step of the process, and the object for destruction obtained from the raw waste or sediment, can be used, of course, as fertilizers for a farm land or a fruit farm, a kitchen garden, a wadi and others, or for food products for domestic animals, such as pigs. In addition, it can be accommodated in the dry combustion furnace 2 and subsequently incinerated as garbage that can be burned.

"Cooling - Step 167" The waste heat obtained from the combustion chamber 17 of the dry combustion furnace 2 is supplied to the freezing machine 63 of the cooling tank portion 9 by means of the circulation tube 30 to operate the freezing machine. 63 so that the liquid stored in the water tank 59 is cooled by an endothermic tube 62. The fresh air passing through the air guide tube 60 inserted in the water tank is cooled, cooling the water tank 59, and the high temperature exhaust in the centrifugal furnaces 35, 48 and 78 can be cooled extremely quickly with the effect of the ejector, when the cold air is blown from the fans 39, 52 and 80 of the smoke feed portions 4 , 7 and 77, respectively, to the ends of the tubes 40a, 53a and 81a of the gas conduits 40 and 81 or the conduit 53. Additionally, the cooling water of the water tank 59 is used to cool the water. circulation tube 64 inserted into the cooling apparatus and the like, and cold air or cold water can be used for the cooling apparatus, except the multifunctional destruction apparatus 1 and the. In an area of heavy snow, snow, ice or cold water may be stored in a tank or water tank and in an appropriate amount thereof, it may be introduced into the inlet opening 59a of the water tank 59 in accordance with the needs. Figure 15 is a flow chart showing a method for melting expanded polystyrene, polymer-based substances and others, using the multifunctional destruction apparatus of the present invention. The processing method of this example converts the expanded polystyrene, the polymer-based substances and others, into a solid material that is to be reused, without generating gases or hazardous substances.

"Expanded Polystyrene Introduction Process 171" The expanded polystyrene / polymer based substance 27 is accommodated in the melting tank 26 of the casting apparatus 10 of the multifunctional destruction apparatus, shown in Figure 2.

"Heating - Step 172" The heating burner 55 of the air drying portion 8, illustrated in Figure 5 is turned on, or the heat radiator 68 of the air drying portion 8 shown in Figure 6, is operated . At the same time, the opening / closing valve 58a of the air supply tube 58 is opened, and the opening / closing valve 61b of the air cooling tube 61 of the cooling tank portion 9 and the opening valve / Closing 22a of the air supply pipe 22 of the dry combustion furnace 2, are closed.

"Casting - Step 173" The opening / closing valves 25a and 28a connected to the air supply tube 25 and the exhaust pipe 28 connected to the upper and lower portions of the casting apparatus 10, are open to conduct the hot air of the heating burner 55 coming from the air supply tube 25. The expanded polystyrene 27 accommodated in the melting tank 26 is melted by the hot air, and the polystyrene and the substances based on liquid polymers are filtered through the grating of the grate plate 26 and penetrate to be deposited in the tray 26b.

"Collection - Step 174" The tray 26b accommodated in the smelting tank 26 is taken out of the smelting tank 26. The liquid polystyrene, the polymer-based substance and others, can be reused. The hot air that melted the expanded polystyrene 27, the polymer-based substance and others, pass through the gas channel 28 to be conducted into the gas conduit 47. Then it is no longer melted in the second smoke feed portion 7. to be emitted from conduit 53 to the exterior of the multifunctional destruction apparatus 1. Figure 26 is a flow chart showing the method for melting the incinerated ash using the multifunctional destruction apparatus according to the present invention. The processing method of this example converts the incinerated ash into a solid material to be reused.

"Introduction of Incinerated Ash - Step 175" The incinerated ash is introduced into the crucible 74 mounted on the refractory brick 74b in the ash melting furnace 72 of the ash casting portion 7 of the multifunctional destruction apparatus 1 illustrated in Figure 2.

"Heating - Step 176" The heating burner 73 placed in the ash cast portion 72, shown in Figure 7 is ignited to be heated to a high temperature of about 1300 ° C to 1800 ° C. The high temperature is obtained by the heat stored in the crucible 74 and the inner wall of the crucible 74. That is, when the bricks and the like are placed around the crucible 74, it is possible to obtain a high temperature by the effect of thermal storage. The placement of bricks, runners and other materials around the crucible can achieve the high temperature. Further, since the tip of the burner 73 is positioned upwardly, the flame uniformly heats spirally the peripheral outer surface of the crucible 74, thereby heating, to a high temperature. In addition, heating to high temperature can be achieved by simultaneously incinerating the absorbed exhaust gas entering from the heating burner 73 and the drying oven 3 and the incinerated ash. At this time, when the exhaust gas absorbed and flowing from the drying oven 3 or the dry incineration oven 2 is burned, the exhaust gas is reduced and the unburned gas is burned simultaneously. Therefore, incineration at high temperature can be performed by the mixed combustion, which is advantageous to counteract the exhaust gas.

"Casting - Step 177" The incinerated ash, which has been introduced into the crucible 74 to have a high temperature of 1300 ° C to 1800 ° C, is melted to puddling. In other words, glass, lava and other materials have melted.

"Collection - Step 178" The cover 72a is opened to see that the glass, lava and other materials are melted in the crucible 74, and are removed.

"Cooling - Step 179" The incinerated ash removed from crucible 74 is cooled using cooling water or air.

"Hardening - Step 180" When the cast has hardened by applying cold water to it or using air, it is hardened in a manner similar to irregular marble. Said hardened incinerated ash can be mixed with gravel or cement for building materials, to be used again. Figure 17 is a partial cross-sectional view of another embodiment of the multifunctional destruction apparatus according to the present invention, showing the condition where a cylindrical tube is placed in the dry chamber. That is, as illustrated in Figure 17, a drying apparatus 2a is installed in the second dry chamber 15b. This is a device that passes the raw waste, general waste and sediment and others through the drying apparatus 2a and dries them indirectly by the heat of combustion generated from the combustion chamber 17. This drying apparatus 2a can be installed in any of the dry chambers 15, 15b, and 15d, respectively. Figure 18 is a cross-sectional view showing the installation of the drying apparatus illustrated in Figure 17. As illustrated in Figure 18, a worm conveyor 2c is rotatably installed in the cylindrical drying tube 2b, in which the inlet opening 2e is formed, and the drying apparatus 2a is heated by the high heat of the combustion chamber 17 to perform the drying while the raw waste, the general waste, the sediment and other objects 2f introduced from the entrance opening 2e are transferred by the worm conveyor 2c. Figure 19 is a cross-sectional view showing another embodiment of the drying apparatus. In the drying apparatus 2a of this example, the raw garbage, the general garbage, the sediment and other objects 2f introduced from the entrance opening 2e are moved using a 2g belt conveyor in the cylindrical drying tube 2b, instead of use the auger conveyor 2b. Irregularities are formed on the surface of the belt conveyor 2g. These irregularities facilitate the transfer of the object to be dried 2d. Figure 20 is a cross-sectional view showing still another embodiment of the drying apparatus. In the drying apparatus 2a of this example, the toothed bands 2j and 2k are installed in the horizontal direction of the cylindrical drying tube 2b, and the driving wheels 2h and 2i are provided in the positions where they are engaged with the toothed bands 2j and 2k. When the driving wheels 2h and 2i rotate, the cylindrical drying tube 2b rotates, and the object to be dried 2d in the cylindrical drying tube 2b moves towards the driving wheel 2h on the left side. Irregular spiral grooves are formed in the peripheral inner surface of the cylindrical drying tube 2b and the object to be dried 2d is moved therefrom. Figure 21 is a partial cross-sectional view showing a further embodiment of the multifunctional destruction apparatus of the present invention. In the multifunctional destruction apparatus of this example, a plurality of air vents 15h are formed on the interior surface of the dry chambers 15, 15a, 15d, and 15f and the combustion chamber 17, a check valve 22a is installed on the the air supply tube 22. Furthermore, a sealing member 174 is installed on the shaft of a vibrator 17a. The installation of the sealing member 17e does not cause the heat of the chamber 17e to be diffused. As illustrated in Figure 25, the air vent 15h is formed in the longitudinal direction. Figure 22 is a longitudinal cross-sectional view of the check valve connected in Figure 21, illustrating the closed condition thereof. As illustrated in Figure 22, the check valve 22a is constituted by a valve 22b and a plug 22c. That is, the valve 22b is adapted to have the ability to rotate in the air supply tube 22 as indicated by an arrow, and the plug 22c is fixed to the lower left position of the valve 22b. When the valve 22b is in such condition, the air supply is stopped in the air supply tube 22. Figure 23 is a longitudinal cross-sectional view of a check valve installed in Figure 21, showing the open condition Of the same. As illustrated in Figure 23, when the valve 22 is sealed to the interior surface of the air supply tube 22, air is supplied from the direction of the plug 22c.

Figure 24 is a partial cross-sectional view showing still a further embodiment of the multifunctional destruction apparatus of the present invention. In the multifunctional destruction apparatus of this example, a burner 31e is provided for the drying oven 3. In such a way that the installation of the burner 31e to the drying oven 3, can perform efficient drying.

POSSIBILITY OF INDUSTRIAL USE As the present invention has the structure described above, the following advantages can be obtained. First, taking into account the post-incineration uses, the incineration time and others, processes can be selected to be carried out without generating dangerous substances. Second, with the use of the expiration effect of the expeller or drying with cold air, the odor and dioxins can be suppressed at the maximum level. Third, the waste heat obtained from the combustion heat generated in the combustion chamber can heat the air or the hot stream, and the freezer and boiler can be operated using waste heat to be used for air conditioning from other facilities.

Fourth, when pollution and burned matter containing hazardous substances such as dioxins or gases are injected, oxidative combustion and smoke combustion can be advanced simultaneously, thereby pyrolysing dangerous substances to be deactivated. Fifth, when the substances based on polymers or gases, with which the combustion object can be burned at a high temperature, are injected and mixed with the PCBs and others, so that a temperature range reaches several thousand ° C, PCBs and others can be pyrolyzed in the reduced atmosphere to be deactivated. Sixth, when the introduced combustion object defined in the claims is mixed and incinerated, detoxification becomes possible. Since this combustion system can incinerate dioxins and others by pyrolization, leaving no unburned material in the ash incinerated by combustion in the reduced atmosphere at a temperature of 450 ° C, dioxins and others can be pyrolyzed by mixing the waste containing a large amount of dioxins and others, in conventional material incinerated with waste material, incinerated conventional ash and soil contamination (materials containing dioxin) to be incinerated so that oxidative combustion and smoke combustion are performed simultaneously, dioxins and other substances can be pyrolyzed. This incineration system does not produce dioxins by pyrolysis in the combustion process nor does it produce dioxins in the incinerated ash, because it is pyrolyzed in the reduced atmosphere. Seventh, even if the raw waste, sediment, expanded polystyrene, polymer, general waste, and other objects are mixed, the non-combustible material can be dried or the polymer, polystyrene and others can be charred. Said processes can be halted, and the drying, carbonization and incineration can be carried out finally without restriction. When the multifunctional destruction apparatus according to the present invention is placed in parallel or in series, the operation of a continuous plant can be enabled.

Claims

NOVELTY OF THE INVENTION Having described the present invention, it is considered as novelty, and therefore, the content of the following is claimed as property: CLAIMS

1. A multifunctional destruction apparatus which comprises: a dry combustion furnace; a drying oven; a first portion of smoke feed; a second portion of smoke feed; a portion of smoke combustion; a portion of dust filter; a second portion of smoke feed; a portion of air heating; a cooling tank portion, wherein an air flow is generated in a direction from said cooling tank portion to said second smoke feed portion to form a vacuum.

2. The multifunction destruction apparatus according to claim 1, wherein a drying apparatus having a cylindrical drying tube is installed in a dry chamber of said dry combustion chamber for the purpose of indirect drying.

3. The multifunction destruction apparatus according to claim 1, wherein a heat radiator installed at one end of a heat pipe and the like, having a parabola condenser connected at the other end thereof, is provided in the heating chambers of said dry combustion chamber, said smoke combustion chamber and said air heating portion.

4. The multifunction destruction apparatus according to claim 3, wherein a lens condenser and a parabola condenser are connected to said heat pipe.

5. The multifunction destruction apparatus according to claim 3 or 4, wherein the source energy to operate a fan, a burner, a freezing machine and a conveyor, the rotation of a vibrator, a dry plate and a grate plate, the opening / closure of an opening / closing valve and the operation of artificial cooling is a generation of wind energy.

6. The multifunction destruction apparatus according to claim 3, 4, or 5, wherein said energy source is a generation of solar energy.

7. The multifunction destruction apparatus according to claim 1, wherein an ash melting furnace is installed in the rear part of said drying furnace and said dry combustion portion and a centrifugal furnace are installed in said ash melting furnace.