KR102447973B1 - Pollution free incinerator using combustible waste - Google Patents

Abstract

The present invention relates to a pollution free incinerator for combustible waste, comprising: a furnace body having a combustion space into which combustible waste is put; a first unit mounted on one side of the furnace body in a replaceable and separable manner, and having at least one filter element incorporating a catalyst to filter hazardous substances, including dioxins, incombustible ashes, and volatile organic compounds, contained in the combustion gas generated from combustible waste incinerated in the combustion space; and a second unit including a funnel which is connected to the combustion space via the first unit and has a passage discharging exhaust gas filtered while passing through a combustion gas filter element into the air, and a heat exchanger which is formed around the funnel to recover heat from the exhaust gas discharged through the funnel. The present invention is eco-friendly since incinerating combustible waste simply regardless of places and discharging the exhaust gas purified, and can utilize recovered waste heat as energy sources for domestic hot water, heating, agriculture, or manufacturing processes.

Description

Combustible waste pollution-free incinerator {POLLUTION FREE INCINERATOR USING COMBUSTIBLE WASTE}

The present invention relates to a non-polluting incinerator for combustible waste, and more particularly, it is environmentally friendly by incinerating combustible waste regardless of location and discharging it as purified exhaust gas, as well as domestic hot water or heating or agriculture or manufacturing through waste heat recovery. It relates to a non-polluting incinerator for combustible waste that can be used as an energy source for the process.

In the case of synthetic resins or rubbers among industrial wastes or various household wastes, if these are landfilled, they do not rot even after a long time, so there is a problem of contaminating the soil.

In addition, in the case of incineration of these various wastes, harmful substances such as dioxins and volatile organic compounds generated during incineration generate toxic substances harmful to the human body and thus pollute the air. Incineration is strictly prohibited by law, so it is very difficult to dispose of it.

Therefore, the development of technology for the treatment of industrial waste has been promoted as a national project for several decades.

However, due to the development of the industry, the amount of industrial wastes such as synthetic resins and rubbers is increasing.

Conventionally, waste treatment devices for treating industrial wastes or various household wastes as described above have been developed in various structures.

Among them, general incinerators, including “Safe Incinerator for Large-Capacity Garbage and Combustible Waste” (hereinafter referred to as the prior art) of Patent Registration No. 10-0332420, put various wastes into an incinerator made of fireproof material, and then directly heat the waste to create the inside of the incinerator. The waste is incinerated, and the soot generated during incineration is configured to be removed by a separate dust collector.

However, conventional incinerators including the prior art have a problem in that a large-scale and wide construction site is required for the purpose of batch processing of large-capacity wastes generated in large quantities in the suburbs of cities so far.

On the other hand, it is very troublesome to deal with a small amount of combustible waste generated from the daily life and various tasks of a small number of people in a suburban area away from the city, an agricultural complex, or a remote mountainous area.

Therefore, the residents living in these areas are incinerated and disposed of at night secretly in such a small amount of combustible waste.

However, this incineration treatment method not only pollutes the air and soil, but also poses a threat to the health, including the respiratory tract, of the workers performing the incineration operation.

Therefore, incineration of combustible waste generated on a small scale conveniently regardless of location, purifying harmful substances generated during incineration and discharging it as clean exhaust gas, and recovering the heat source generated in the incineration process so that it can be reused in various consumers The development of eco-friendly devices is urgently needed.

Registered Patent No. 10-0332420

The present invention was invented to improve the above problems, and it is environmentally friendly by simply incinerating combustible waste regardless of location and discharging it as purified exhaust gas, as well as living hot water or heating or agriculture or manufacturing through waste heat recovery. This is to provide a non-polluting incinerator for combustible waste that can be used as an energy source for the process.

In order to achieve the above object, the present invention is a furnace body provided with a combustion space into which combustible waste is input; The catalyst is installed to be replaceably and detachably mounted on one side of the furnace body, and to filter harmful substances including dioxins, unburned sludge and volatile organic compounds contained in the combustion gas generated from the combustible waste incinerated in the combustion space. a first unit in which at least one filter body formed by supporting it is built-in; and a communication which communicates with the combustion space through the first unit and forms a flow path through which the combustion gas passes through the filter body and exhausts the filtered exhaust gas to the atmosphere, and is formed around the communication and is discharged through the communication. It will be possible to provide a non-polluting combustible waste incinerator comprising a second unit including a heat exchanger for recovering heat from the exhaust gas.

Here, the filter body is characterized in that it is formed in a block shape having a honeycomb structure by the ceramic mixed with the catalyst.

At this time, the catalyst is at least one or a combination of at least one of TiO2, V2O3, Fe2O3, Pt, and Pd, and the ceramic filter is at least one of Mullite or Cordierite, or a combination of at least one or more characterized in that

In addition, the filter body has a honeycomb structure in which a mullite material made of 3Al2O3 or 2SiO2 and a TiO2 and V2O3 catalyst are mixed to remove the dioxin among the harmful substances, and at least one or more products in the shape of a disk having a certain thickness One filter block and at least one second filter in the shape of a disk having a predetermined thickness and having a honeycomb structure in which a Fe2O3 catalyst is mixed with a mullite material made of 3Al2O3 or 2SiO2 to remove the unburned sludge from among the harmful substances A block and a honeycomb structure in which Pt and Pd catalysts are mixed in a cordierite material made of 2MgO, SiO2, and Al2O3 to remove volatile organic compounds from among the harmful substances, and at least one or more third third It is characterized in that it includes a filter block.

And, a cap including a cover covering the open upper surface of the furnace body, an extension tube extending along an edge of the cover and having an inner circumferential surface facing the upper outer circumferential surface of the furnace body, and fixed to the ceiling surface of the cover It further comprises a container having an upper edge and a bottom surface on which the plurality of filter bodies are seated, wherein the communication is connected to the cover.

In addition, the second unit includes a heat exchange body having an inner diameter greater than an outer diameter of the communication body, accommodating a portion of an outer peripheral surface of the communication communication vertically along the formation direction of the communication body, and disposed on the upper side of the furnace body; a main blower disposed on one side of the to blow out a certain amount of air for a certain period of time, a heat exchange pipe connected to the outlet of the main blower and connected to the outer peripheral surface of the lower side of the heat exchange body, and the outlet of the main blower It is characterized in that it further comprises a combustion pipe connected to the combustion space of the furnace body.

In addition, the second unit includes a distributor connecting the inlet side of each of the heat exchange pipe and the combustion pipe and an outlet of the main blower, and is built in the distributor and disposed on the inlet side of the heat exchange pipe, from the main blower a first damper capable of adjusting the amount of air directed to the heat exchange pipe; It characterized in that it further comprises a waste heat recovery pipe connected to the outer peripheral surface of the upper side of the main blower for supplying a heat exchange gas discharged by heat exchange between the air supplied from the main blower and the exhaust gas inside the communication pipe to a consumer.

In addition, a cyclone dust collector connected to the upper end of the communication, a residual dust collection bag connected to the cyclone dust collector, and an exhaust blower provided on the discharge side of the cyclone dust collector to forcibly discharge the exhaust gas. characterized in that

In addition, the combustible waste is processed in the form of pellets and put into the furnace body, and the combustible waste is pulverized to have a width or length of 5 to 10 mm and processed into the pellet form by rotating the pellet. Drying of the furnace-processed product is characterized in that it is made by waste heat supplied from a waste heat recovery pipe connected to the discharge side of the heat exchanger.

According to the present invention having the above configuration, the following effects can be achieved.

First, the present invention is environmentally friendly because combustible waste is simply incinerated regardless of location and discharged in the form of purified exhaust gas.

In addition, the present invention recovers the heat source generated during incineration of combustible waste and utilizes it as domestic hot water or heating, or as an energy source for agriculture or manufacturing process, and thus has a feature in terms of efficient energy management.

In addition, the present invention is a ceramic filter containing mullite or cordierite together with various catalysts including TiO2, V2O3, Fe2O3, Pt, Pd, etc. to enable filtration by harmful substances generated during incineration of combustible waste, thereby dioxin However, it has the advantage of being able to actively filter and remove each representative hazardous substance such as unburned sludge or volatile organic compounds.

In addition, the present invention has the effect of being able to implement a filter performance excellent in strength and durability structurally while maximizing the filtration area by manufacturing a ceramic filter mixed with various catalysts in a honeycomb structure.

Above all, the present invention can easily incinerate and dispose of a small amount of combustible waste generated from the daily life and various tasks of a small number of people in a suburban area away from the city, an agricultural complex, or a remote mountainous area without being limited by space and time. It is a very useful invention in that it exists.

1 is a conceptual diagram showing the overall structure of a non-polluting incinerator for combustible waste according to an embodiment of the present invention;
FIG. 2 is a conceptual view showing the internal structure of a non-polluting incinerator for combustible waste according to an embodiment of the present invention, as viewed from a point II of FIG. 1 .
3 is a conceptual view showing a partial structure of a second unit, which is a main part of a non-polluting incinerator for combustible waste according to another embodiment of the present invention, as viewed from the point III of FIG. 1 .

Advantages and features of the present invention, and methods of achieving them, will become apparent with reference to the embodiments described below in detail in conjunction with the accompanying drawings.

However, the present invention is not limited to the embodiments disclosed below, but will be implemented in various different forms.

In the present specification, the present embodiment is provided to complete the disclosure of the present invention, and to completely inform those of ordinary skill in the art to which the present invention pertains to the scope of the present invention.

And the invention is only defined by the scope of the claims.

Thus, in some embodiments, well-known components, well-known operations, and well-known techniques have not been specifically described to avoid obscuring the present invention.

In addition, like reference numerals refer to like elements throughout the specification, and terms used (referred to) in this specification are for the purpose of describing the embodiments and are not intended to limit the present invention.

In this specification, the singular also includes the plural unless specifically stated in the phrase, and elements and operations referred to as 'comprising (or having)' do not exclude the presence or addition of one or more other elements and operations. .

Unless otherwise defined, all terms (including technical and scientific terms) used herein may be used with the meaning commonly understood by those of ordinary skill in the art to which the present invention belongs.

Also, terms defined in commonly used dictionary are not to be interpreted ideally or excessively unless defined.

Hereinafter, preferred embodiments of the present invention will be described with reference to the accompanying drawings.

First, FIG. 1 is a conceptual diagram illustrating the overall structure of a pollution-free incinerator for combustible waste according to an embodiment of the present invention.

And, FIG. 2 is a conceptual diagram illustrating the internal structure of a non-polluting incinerator for combustible waste according to an embodiment of the present invention, as viewed from a point II of FIG. 1 .

In addition, FIG. 3 is a conceptual diagram illustrating a partial structure of the second unit 200, which is a main part of a non-polluting incinerator for combustible waste according to another embodiment of the present invention, as viewed from the point III of FIG. 1 .

For reference, an unexplained reference numeral 400 in FIG. 1 indicates an inspection ladder for providing convenience when an operator approaches the upper side of the furnace body 300 for inspection and separate replacement and input installation of the filter body 110 to be described later. .

The present invention is a furnace body 300 provided with a combustion space 301 into which combustible waste (hereinafter not shown) is input as shown, and is mounted on the furnace body 300 and is generated by incineration of combustible waste. The first unit 100 filters harmful substances, and the second unit 200 recovers a heat source generated by incineration of combustible waste, so it can be understood that the structure is reusable.

The first unit 100 is replaceably and detachably mounted on one side of the furnace body 300, and includes dioxins, incombustible sludge, and volatile organic compounds contained in combustion gas generated from combustible waste incinerated in the combustion space 301 . At least one filter body 110 formed by supporting a catalyst to filter harmful substances including

The second unit 200 communicates 210 through the combustion space 301 and the first unit 100, passes through the combustion gas filter body 110, and forms a flow path for discharging the filtered exhaust gas to the atmosphere. 210 and a heat exchanger 220 formed around the communication 210 to recover heat from the exhaust gas discharged through the communication 210 .

It goes without saying that the present invention can be applied to the above-described embodiments, and can also be applied to the following various embodiments.

First, the furnace body 300 is provided to perform the original role of the incinerator to reduce the volume by inputting and incinerating various combustible wastes.

The first unit 100 filters various harmful substances such as dioxins and volatile organic compounds contained in the combustion gas generated by incineration of various combustible wastes through the above-mentioned catalyst and discharges them into the atmosphere in the form of exhaust gas in a clean state. It is provided to perform a filtration function for

The second unit 200 is for energy management and acquisition of an eco-friendly structure, and while discharging clean exhaust gas filtered through the flue 210, recovers high heat of the exhaust gas to heat living or vinyl sewage. Or, it is provided for the purpose of reducing the operating load of the thermal fluid machine for drying and heating of various manufacturing processes.

That is, the second unit 200 prevents the direct discharge of harmful substances into the atmosphere to reduce air pollution, and at the same time reduces the operating load of the boiler or heater to be operated for the various heating and manufacturing processes described above. It will be able to fulfill the role of reducing it sufficiently.

On the other hand, one side of the furnace body 300 is passed through the input slot 302 to put combustible waste, and the input slot 302 is rotatably coupled to a door 310 for entry and exit of the waste to form the input slot 302 . will be able to open

Here, the entry tray 320 is disposed on the bottom surface of the furnace body 300 and can be entered and exited from the outer peripheral surface of the lower side of the furnace body 300, accommodates combustible waste or supports and supports the residue after combustion of combustible waste. .

At this time, the entry and exit handle 321 is provided on one side of the outer peripheral surface of the entry and exit tray 320 to be able to grip, it will be possible to promote the convenience of the operation.

Therefore, the residue such as ash remaining after the incineration of combustible waste is completed is contained in the exit tray 320 as it is, grabs the entry handle 321 , and pulls it from the furnace body 300 to separate the entry tray 320 , and then the remaining The water would have to be landfilled or disposed of.

On the other hand, the combustible waste may be processed in the form of pellets and put into the furnace body 300 .

Combustible wastes contain a wide variety of materials.

Combustible waste includes almost all of the things that occur in the lives of residents, such as paper, plastics, wood, toilet paper, sanitary napkins, diapers, rubber, PET bottles, vinyl, Styrofoam, masks, gloves, clothing, and shoes.

These combustible wastes are pulverized to have a width or length of 5 to 10 mm and processed into pellets by rotating them.

Needless to say, the drying of the pellets processed in this way may be made by waste heat supplied from the waste heat recovery pipe 270 connected to the discharge side of the heat exchanger 220, which will be described later.

Meanwhile, the filter body 110 may be formed in a block shape having a honeycomb structure as shown in the enlarged part of FIG. 2( b ) by a ceramic mixed with a catalyst.

Here, the catalyst is at least one or a combination of at least one of TiO2, V2O3, Fe2O3, Pt, and Pd, and the ceramic filter is at least one or a combination of at least one or more of Mullite or Cordierite. .

TiO2, V2O3, and FeO3 catalysts may be mixed in the mullite at a ratio of about 10-30w/w%.

The Pt and Pd catalysts may be mixed with cordierite in a ratio of 1 to 10w/w%, and cordierite may be composed of 13% 2MgO, 50% SiO2, and 35% Al2O3.

Meanwhile, the filter body 110 may include first, second, and third filter blocks 111 , 112 , and 113 as shown in FIG. 2 .

That is, the first filter block 111 has a honeycomb structure in which TiO2 and V2O3 catalysts are mixed in a mullite material made of 3Al2O3 or 2SiO2 in order to remove dioxins among harmful substances, and at least one or more discs having a predetermined thickness. is absent

In addition, the second filter block 112 has a honeycomb structure in which a Fe2O3 catalyst is mixed with a mullite material made of 3Al2O3 or 2SiO2 in order to remove unburned sludge among harmful substances, and at least one or more discs having a predetermined thickness. is absent

In addition, the third filter block 113 has a honeycomb structure in which Pt and Pd catalysts are mixed in a cordierite material made of 2MgO, SiO2 and Al2O3 to remove volatile organic compounds from harmful substances, and has a disk shape having a certain thickness. is at least one member.

In the present invention, as shown in FIG. 2(b), two first filter blocks 111 are disposed and the second filter blocks 112 and third filter blocks 113 are disposed one by one. It is not limited to the structure and the number of batches.

For example, depending on the type of combustible waste to be incinerated, the number of the first filter block 111 may be increased to increase the number of the first filter block 111 as shown in the case of a large amount of dioxin emission, or the second filter block ( 112) by increasing the number, or by increasing the number of volatile organic compounds to be discharged, various applications and modifications such as increasing the number of the third filter block 113 will be possible.

On the other hand, the first unit 100 may be applied to an embodiment of the structure further comprising the cap 120 and the housing tube 130 that are seated and fixed while covering the open upper surface of the furnace body 300 .

The cap 120 includes a cover 121 covering the open upper surface of the furnace body 300 and an extension tube 122 extending along the edge of the cover 121 and having an inner peripheral surface facing the upper outer peripheral surface of the furnace body 300 . ) may be included.

The container 130 has an upper edge fixed to the ceiling surface of the cover 121 and a bottom surface on which the plurality of filter bodies 110 are seated as shown in FIG. 2(a).

Accordingly, it can be understood that the communication 210 is connected to the cover 121 through the communication hole 150 to be described later.

On the other hand, the first unit 100, the gas cylinder slot 131 and the management means ( 140) and the communication hole 150 may be further provided.

The gas cylinder slot 131 is a disk-shaped plurality of filter bodies 110 having a predetermined thickness are radially disposed on the bottom surface of the receiving cylinder 130, so that the combustion gas passes through the filter body 110, the filter The sieve 110 is to be penetrated at a position corresponding to the bottom surface of each.

The management means 140 is rotatably coupled to the replacement slot 141 and the replacement slot 141 having a semicircular shape penetrating through the upper surface of the cover 121 corresponding to the positions where the plurality of filter bodies 110 are disposed, respectively. It is to include a replacement tab 142 to open and close the replacement slot (141).

The communication hole 150 is passed through the center of the cover 121 to connect the inner space of the filter container 130 and the communication 210 .

Here, the diameter of the replacement slot 141 having a semicircular shape is preferably formed to be larger than the diameter of each of the filter bodies 110 for smooth input installation and separation replacement of the filter bodies 110 .

At this time, the first unit 100 is formed on the upper surface of the inspection and replacement tab 142 and further includes a grippable rotation handle 143 , when it is necessary to replace the filter body 110 or the container 130 . ) If an internal inspection is required, it will be possible to provide convenience to the operator to open the inspection and replacement tab 142 by holding and lifting.

In addition, the first unit 100 is formed to protrude from the bottom surface of the accommodating cylinder 130 along the outer edge of the gas cylinder and the slot 131 , and has an inner diameter greater than the outer diameter of each filter body 110 and the filter body ( 110) It may further include a filter mounting wall 132 having a height smaller than each thickness.

On the other hand, the second unit 200, which constitutes the heat exchanger 220, has an inner diameter larger than the outer diameter of the communication 210 and up and down along the formation direction of the communication 210, a portion of the outer peripheral surface of the communication 210 It accommodates and may further include a heat exchange body 221 disposed on the upper side of the furnace body 300 .

Here, the second unit 200 is disposed on one side of the furnace body 300 and is connected to the main blower 230 (main blower) that blows out a certain amount of air for a certain time, and the outlet of the main blower 230 to heat exchange. It further includes a heat exchange pipe 240 connected to the outer peripheral surface of the lower side of the body 221, and a combustion pipe 250 connected to the outlet of the main blower 230 and connected to the combustion space 301 of the furnace body 300. you might be able to

In this case, as shown in FIG. 3(b) , manual air supply means such as bellows 290 may be used, as shown in FIG.

On the other hand, the second unit 200, as shown in FIG. 3, a distributor 260 connecting the inlet side of each of the heat exchange pipe 240 and the combustion pipe 250 and the outlet of the main blower 230, and the distributor 260. It goes without saying that the first and second dampers 261 and 262 built in the , and a waste heat recovery pipe 270 connected to the heat exchange body 221 may be further provided.

First, the first damper 261 is built into the distributor 260 and disposed on the inlet side of the heat exchange pipe 240 , and is provided to control the amount of air directed from the main blower 230 toward the heat exchange pipe 240 .

In addition, the second damper 262 is built in the distributor 260 and disposed on the inlet side of the combustion pipe 250 , and is provided to control the amount of air directed from the main blower 230 toward the combustion pipe 250 .

In addition, the waste heat recovery pipe 270 is connected to the outer peripheral surface of the upper side of the heat exchange body 221 so that the air supplied from the main blower 230 and the exhaust gas inside the communication pipe 210 exchange heat and supply the heat exchange gas discharged to the consumer. It is designed to fulfill its role.

On the other hand, according to the present invention, the discharge side of the cyclone dust collector 280 connected to the upper end of the communication tube 210, the residual dust collecting bag 281 and the cyclone dust collector 280 connected to the cyclone dust collector 280 It may further include an exhaust blower (not shown below) provided in the forcibly discharging exhaust gas.

The cyclone dust collector 280 is for capturing a small amount of residual fine dust contained in the exhaust gas discharged through the flue 210 even in an emergency, and since it is a known technology, its internal structure and detailed operation mechanism will be described. omit

Therefore, the residual fine dust is collected in the residual dust collecting bag 281 connected to the cyclone dust collector 280, and the exhaust gas that has been reliably purified is discharged to the atmosphere, but if an exhaust blower is installed, the airflow accumulation is prevented by forcibly discharging to the atmosphere. will be able to solve

As described above, the present invention is environmentally friendly by incinerating combustible wastes regardless of location and discharging them as purified exhaust gas, as well as hot water or heating for living through waste heat recovery, or energy sources for agriculture or manufacturing processes. It can be seen that the basic technical idea is to provide a non-polluting incinerator for combustible waste.

And, within the scope of the basic technical spirit of the present invention, many other modifications and applications are also possible for those of ordinary skill in the art.

100...first unit
110... filter body
111...first filter block
112...Second filter block
113...3rd filter block
120...caps
121...cover
122... toolbox
130...receptacle
131...gas cylinder and slot
132...Filter mounting wall
140...Management measures
141...replacement slot
142...Check and replace tab
143...Swivel handle
150...Communication Hall
200...2nd unit
210...
220...heat exchanger
221...heat exchange body
230...Main blower
240...heat exchange piping
250...combustion piping
260...Distributor
261...first damper
262...Second damper
270...Waste heat recovery piping
280...cyclone dust collector
281...Residual dust collection bag
290... Bellows
300 furnace body
301...combustion space
302...Input Slot
310...Waste entrance door
320...Access tray
321...Access handle
400...check ladder

Claims (9)

a furnace body having a combustion space into which combustible waste is input;
The catalyst is installed to be replaceably and detachably mounted on one side of the furnace body, and to filter harmful substances including dioxins, unburned sludge and volatile organic compounds contained in the combustion gas generated from the combustible waste incinerated in the combustion space. a first unit in which at least one filter body formed by supporting it is built-in; and
A communication that communicates with the combustion space through the first unit and forms a flow path through which the combustion gas passes through the filter body and exhausts the filtered exhaust gas to the atmosphere, and is formed around the communication and discharged through the communication. and a second unit including a heat exchanger for recovering heat from the exhaust gas,
The filter body,
At least one first filter block in the shape of a disk having a predetermined thickness and having a honeycomb structure in which TiO2 and V2O3 catalyst are mixed in a mullite material made of 3Al2O3 or 2SiO2 in order to remove the dioxin from among the harmful substances;
At least one second filter block having a honeycomb structure in which a Fe2O3 catalyst is mixed with a mullite material made of 3Al2O3 or 2SiO2 in order to remove the unburned sludge among the harmful substances, and having a disk shape having a certain thickness;
In order to remove volatile organic compounds from among the harmful substances, it has a honeycomb structure in which Pt and Pd catalysts are mixed in a cordierite material made of 2MgO, SiO2 and Al2O3, and at least one third filter block in the shape of a disk having a certain thickness. including,
The first unit is
a cap including a cover covering the open upper surface of the furnace body, and an extension tube extending along an edge of the cover and having an inner circumferential surface facing the upper outer circumferential surface of the furnace body;
A receiving passage having an upper edge fixed to the ceiling surface of the cover and a bottom surface on which the plurality of filter bodies are seated;
As a plurality of the filter bodies in the shape of a disk having a predetermined thickness are radially disposed on the bottom surface of the container, the combustion gas passes through the filter body so as to pass through at a position corresponding to the bottom surface of each filter body gas cylinders and slots;
Management means including a replacement slot having a semicircular shape penetrating through the upper surface of the cover corresponding to a position where the plurality of filter bodies are disposed, respectively, and an inspection replacement tab rotatably coupled to the replacement slot to open and close the replacement slot; ,
a communication hole passing through the center of the cover to connect the communication with the inner space of the filter container;
a rotation handle formed on the upper surface of the inspection and replacement tab and capable of gripping;
Further comprising a filter mounting wall protruding from the bottom surface of the housing along the outer edge of the gas cylinder and the slot, having an inner diameter larger than the outer diameter of each of the filter bodies and having a height smaller than the thickness of each of the filter bodies,
The communication is connected to the cover,
A non-polluting combustible waste incinerator, characterized in that the semi-circular shape of the replacement slot is formed to be larger than the diameter of each of the filter bodies.
The method according to claim 1,
The filter body is a combustible waste pollution-free incinerator, characterized in that formed in a block shape having a honeycomb structure by the ceramic mixed with the catalyst.
3. The method according to claim 2,
The catalyst is at least one or a combination of at least one of TiO2, V2O3, Fe2O3, Pt, and Pd,
The ceramic filter is a combustible waste pollution-free incinerator, characterized in that at least one or a combination of at least one of mullite or cordierite (Codierite).
delete delete The method according to claim 1,
The second unit is
a heat exchanger body constituting the heat exchanger, having an inner diameter larger than the outer diameter of the communication body, accommodating a part of the outer peripheral surface of the communication communication vertically along the formation direction of the communication communication body, and disposed on the upper side of the furnace body;
a main blower disposed on one side of the furnace body to blow out a certain amount of air for a certain period of time;
a heat exchange pipe connected to the outlet of the main blower and connected to the outer peripheral surface of the lower side of the heat exchange body;
Pollution-free incinerator for combustible waste, further comprising a combustion pipe connected to the outlet of the main blower and connected to the combustion space of the furnace body.
7. The method of claim 6,
The second unit is
a distributor connecting an inlet side of each of the heat exchange pipe and the combustion pipe to an outlet of the main blower;
a first damper built in the distributor and disposed on the inlet side of the heat exchange pipe, the first damper capable of adjusting the amount of air directed from the main blower toward the heat exchange pipe;
a second damper built in the distributor and disposed on the inlet side of the combustion pipe, the second damper being able to adjust the amount of air from the main blower toward the combustion pipe;
Combustible waste pollution-free, characterized in that it further comprises a waste heat recovery pipe connected to the outer peripheral surface of the upper side of the heat exchange body to supply the heat exchange gas discharged by heat exchange between the air supplied from the main blower and the exhaust gas inside the communication tube to a customer. incinerator.
The method according to claim 1,
a cyclone dust collector connected to the upper end of the communication;
and a residual dust collecting bag connected to the cyclone dust collector;
Pollution-free incinerator for combustible waste, which is provided on the discharge side of the cyclone dust collector and further comprises an exhaust blower for forcibly discharging the exhaust gas.
The method according to claim 1,
The combustible waste is processed in the form of pellets and put into the furnace body,
The combustible waste is pulverized to have a width or length of 5 to 10 mm and processed into the pellet form by rotating, and the drying of the processed pellet form is supplied from a waste heat recovery pipe connected to the discharge side of the heat exchanger. Combustible waste pollution-free incinerator, characterized in that made by waste heat.

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