KR102646938B1 - Garbage complete decomposition recycling disposal device for carbon neutrality using pyrolysis gasification - Google Patents

Abstract

The complete waste decomposition recycling treatment device using pyrolysis gasification for carbon neutrality of the present invention includes an input part into which waste is input, a pyrolysis chamber for pyrolyzing the input waste, and the fuel gas generated by pyrolysis in the pyrolysis chamber at an ultra-high temperature. It includes an ultra-high temperature gasification chamber for gasification, and a gas supply pipe for supplying fuel gas from the pyrolysis chamber to the ultra-high temperature gasification chamber.

Description

Waste complete decomposition and recycling treatment device using pyrolysis gasification for carbon neutrality {GARBAGE COMPLETE DECOMPOSITION RECYCLING DISPOSAL DEVICE FOR CARBON NEUTRALITY USING PYROLYSIS GASIFICATION}

The present invention relates to a complete decomposition and recycling treatment device for waste using pyrolysis gasification for carbon neutrality. More specifically, the complete decomposition and recycling treatment of waste using pyrolysis gasification, which can treat waste in an environmentally friendly manner using pyrolysis and high-temperature gasification. It's about devices.

In general, waste includes household waste or various wastes discharged from various industrial fields or households, and the method of disposing of such waste is mainly to remove the waste by burning it using a flame in an incinerator equipped with an incinerator. .

However, the method of disposing of waste by incineration is to directly apply flame to the waste. Due to various factors such as the load, density, moisture content, incinerator size, and heating temperature of the waste, complete combustion is practically impossible, and soot and soot due to incomplete combustion are caused. There is a problem in that a large amount of dust, air pollution, and exhaust gases are generated. In particular, there was a problem with the emission of dioxin, a hazardous substance, when incinerating waste consisting of organic compounds.

Dioxin released in this way is classified as an endocrine disruptor because it acts primarily on the estrogen-related endocrine system in the body and is toxic. In consideration of this, methods for pyrolyzing or carbonizing waste in a high temperature and vacuum environment have been disclosed. However, when treating waste using such pyrolysis, a process of creating/maintaining the inside of the pyrolysis device as a vacuum is required during the pyrolysis process. , As a result, there is a problem that the overall device becomes excessively complicated by providing a temperature management device to manage the temperature of the pyrolysis device heated to a high temperature.

The technical problem to be achieved by the present invention is to provide a recycling treatment device for complete decomposition of waste using pyrolysis gasification for carbon neutrality, which can treat waste in an environmentally friendly manner using pyrolysis gasification.

The problems to be solved by the present invention are not limited to the problems mentioned above, and other problems not mentioned can be clearly understood by those skilled in the art from the description below.

A waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality according to an embodiment of the present invention includes an input part into which waste is input, a pyrolysis chamber for pyrolyzing the input waste, and fuel generated by pyrolysis in the pyrolysis chamber. It includes an ultra-high temperature gasification chamber that gasifies gas at an ultra-high temperature, and a gas supply pipe that supplies fuel gas from the pyrolysis chamber to the ultra-high temperature gasification chamber.

According to the embodiment, the input unit further includes a conveyor unit that transfers the waste introduced into the input unit to the pyrolysis chamber, and a screw part that extends from the conveyor unit and rotates to allow the waste to be supplied into the pyrolysis chamber. It can be included.

Depending on the embodiment, the pyrolysis chamber may include a pyrolysis space in which waste input from the input unit is disposed, a fuel pump that discharges highly flammable liquid fuel into the pyrolysis space, and an ignition unit that provides a flame to the pyrolysis space. You can.

Depending on the embodiment, the pyrolysis chamber may further include a shielding member that blocks or opens the waste movement path between the input unit and the pyrolysis chamber.

Depending on the embodiment, the pyrolysis space is sealed from the outside to maintain low-oxygen conditions during the pyrolysis period, and the ignition unit may provide the flame to the waste only during a preset time for initial ignition.

According to the embodiment, it further includes a first discharge unit for discharging combustion residues generated after pyrolysis in the pyrolysis chamber to the outside, and a second discharge unit for discharging combustion residues generated after combustion in the ultra-high temperature gasification chamber to the outside. can do.

According to the embodiment, the ultra-high temperature gasification chamber consists of first and second connecting members made of a pipe body and in contact with each other to provide an ultra-high temperature gasification space, and is disposed at the center of the rear end of the second connecting member to gasify the fuel gas at ultra-high temperature. It may include an injection nozzle that injects into the space, and a high-pressure gas supply unit that guides the high-pressure gas provided from the compressor to the ultra-high temperature gasification space and generates spontaneous ignition by diffusion with the fuel gas.

According to the embodiment, the ultra-high temperature gasification chamber controls the amount of air inflow into the ultra-high temperature gasification space by adjusting the vent formed in the rear end wall of the second connecting member and the plate-shaped adjustment member disposed on the outside opposite to the vent. It may further include a flow rate control unit.

According to the embodiment, the high-pressure gas supply unit includes a high-pressure gas inlet for introducing high-pressure gas provided from the compressor into one side of the first connecting member, and a high-pressure gas inlet flowing through the high-pressure gas inlet through the air amplification induction path. It may include a high-pressure gas inflow chamber supplied to the ultra-high temperature gasification space.

According to the embodiment, the ultra-high temperature gasification chamber is connected to the tip of the first connecting member, guides the direction of movement of the flame generated in the ultra-high temperature gasification space, and provides a path through which combustion residues of the fuel gas are discharged. Additional guides may be included.

The present invention can treat waste in an environmentally friendly manner by secondary combustion of waste using pyrolysis and high-temperature gasification.

The effects of the present invention are not limited to the effects mentioned above, and other effects not mentioned will be clearly understood by those skilled in the art from the description below.

Figure 1 is a perspective view of a waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality according to an embodiment of the present invention.
Figure 2 is a cross-sectional view of a waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality according to an embodiment of the present invention.
Figure 3 is a perspective view of an ultra-high temperature gasification chamber according to an embodiment of the present invention.
Figure 4 is a cross-sectional view of an ultra-high temperature gasification chamber according to an embodiment of the present invention.
Figure 5 is an exploded perspective view of a flow rate control unit according to an embodiment of the present invention.

The advantages and features of the present invention and methods for achieving them will become clear by referring to the embodiments described in detail below along with the accompanying drawings. However, the present invention is not limited to the embodiments disclosed below and may be implemented in various different forms. The present embodiments are merely provided to ensure that the disclosure of the present invention is complete and to provide a general understanding of the technical field to which the present invention pertains. It is provided to fully inform the skilled person of the scope of the present invention, and the present invention is only defined by the scope of the claims.

The terminology used herein is for describing embodiments and is not intended to limit the invention. As used herein, singular forms also include plural forms, unless specifically stated otherwise in the context. As used in the specification, “comprises” and/or “comprising” does not exclude the presence or addition of one or more other elements in addition to the mentioned elements. Like reference numerals refer to like elements throughout the specification, and “and/or” includes each and every combination of one or more of the referenced elements. Although “first”, “second”, etc. are used to describe various components, these components are of course not limited by these terms. These terms are merely used to distinguish one component from another. Therefore, it goes without saying that the first component mentioned below may also be a second component within the technical spirit of the present invention.

Unless otherwise defined, all terms (including technical and scientific terms) used in this specification may be used with meanings commonly understood by those skilled in the art to which the present invention pertains. Additionally, terms defined in commonly used dictionaries are not interpreted ideally or excessively unless clearly specifically defined.

Figure 1 is a perspective view of a waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality according to an embodiment of the present invention, and Figure 2 is a waste complete decomposition recycling using pyrolysis gasification for carbon neutrality according to an embodiment of the present invention. This is a cross-sectional view of the processing device.

Referring to Figures 1 and 2, the waste complete decomposition recycling treatment device (10, hereinafter referred to as "garbage treatment device") using pyrolysis gasification for carbon neutrality according to an embodiment of the present invention has an input portion ( 100), a pyrolysis chamber 200 that pyrolyzes the input waste, an ultra-high temperature gasification chamber 300 that gasifies the fuel gas generated after pyrolysis in the pyrolysis chamber 200 at an ultra-high temperature, and an ultra-high temperature gasification chamber 300 that gasifies the fuel gas generated in the pyrolysis chamber 200 at an ultra-high temperature. The gas supply pipe 250 that supplies to the gasification chamber 300, the first discharge part 400 that discharges to the outside combustion residues generated after thermal decomposition in the pyrolysis chamber 200, and complete decomposition in the ultra-high temperature gasification chamber 300. It includes a second discharge unit 500 that discharges the fuel gas to the outside, and a compressor 600 that supplies high-pressure gas to the ultra-high temperature gasification chamber 300.

If complete combustion is not achieved when incinerating waste, a large amount of soot, dust, and air pollution emissions are generated due to incomplete combustion, and dioxin, a hazardous substance, may also be emitted. Dioxin is generated by incomplete combustion of waste, and dioxin can also be completely decomposed at temperatures above 1400℃.

Garbage refers to combustible waste and may include waste synthetic rubber, plastic packaging, waste synthetic polymer compounds, waste synthetic resin, waste tires, waste foamed synthetic resin, waste fishing nets, waste wood, SRF, medical waste, etc.

The waste disposal device 10 according to an embodiment of the present invention thermally decomposes waste at a temperature of 200°C to 800°C under low oxygen conditions in the pyrolysis chamber 200, and heats the fuel gas generated by the pyrolysis into the ultra-high temperature gasification chamber 300. By gasifying it at extremely high temperatures of over 1400℃, it enables complete combustion of pollutants such as dioxin generated when incinerating waste.

Ash generated after pyrolyzing waste in the pyrolysis chamber 200 may be discharged to the outside through the discharge unit. Ash is environmentally harmless and can be used as construction materials, etc., and does not require separate landfill costs, thereby realizing an eco-friendly waste disposal device (10).

Table 1 shows the results of testing the pollutant emissions when waste was pyrolyzed and gasified using the waste disposal device 10 according to an actual embodiment of the present invention.

pollutant

Emission allowance
reference value

test results
Primary

Secondary
3rd
4th
dust
20mg/ ^Sm3

4mg/ ^Sm3

5mg/ ^Sm3
6mg/ ^Sm3
4mg/ ^Sm3
C.O.

50 ppm
8 ppm
12ppm
10 ppm
12ppm
SO ₂

30ppm
5 ppm
8 ppm
6ppm
5ppm
NO ₂

70ppm
12ppm
15ppm
18ppm
12 ppm
HCl

15ppm
5ppm
6 ppm
5ppm
3ppm
cadmium

0.020mg/ ^Sm3
0.005mg/ ^Sm3
0.006mg/ ^Sm3
0.005mg/ ^Sm3
0.007mg/ ^Sm3
lead

0.200mg/ ^Sm3
0.040mg/ ^Sm3
0.050mg/ ^Sm3
0.030mg/ ^Sm3
0.030mg/ ^Sm3
Mercury

0.100mg/ ^Sm3
0.020mg/ ^Sm3
0.030mg/ ^Sm3
0.020mg/ ^Sm3
0.090mg/ ^Sm3
arsenic

0.500ppm
0.110 ppm
0.080 ppm
0.070ppm
0.090ppm
smoke
Below 2 degrees
1 degree or less
1 degree or less
1 degree or less
1 degree or less

Referring to Table 1 above, it can be seen that when waste is pyrolyzed and gasified using the waste disposal device 10 according to an embodiment of the present invention, the amount of pollutants emitted is drastically reduced.

The input unit 100 is formed to extend from the conveyor unit 110 and the conveyor unit 110 for transporting the input waste to the pyrolysis chamber 200, and includes a screw unit ( (not shown) may be included.

The conveyor unit 110 may include a belt through which waste is transported, a pulley that rotates the belt, and a motor that transmits power to the pulley. That is, the motor receives power and transmits power so that the pulley rotates, and the belt is linked to the pulley and can rotate and move according to the rotation direction of the pulley.

Garbage introduced into the input unit 100 may fall onto the belt of the conveyor unit 110, and the waste may be transferred to the screw unit by a belt moving in one direction by a motor and pulley, and the waste is pyrolyzed by the screw unit. It may be supplied inside the room 200.

Depending on the embodiment, the screw unit may further include screw wings that protrude in a spiral shape on the inner surface, and waste may be transported to the pyrolysis chamber 200 along the inner wall of the screw unit by the screw wings. That is, the waste transported through the conveyor unit 110 may be located on the screw blade and may be supplied into the pyrolysis chamber 200 along the screw blade formed in a spiral shape along the inner wall of the screw unit.

At this time, the waste transported through the conveyor unit 110 is sequentially placed on the screw wings, and as it is placed on the screw wings, it pushes other waste already placed on the screw wings. Through this method, waste can be located along the screw blades to the upper part of the screw portion, and can finally be supplied into the pyrolysis chamber 200.

Additionally, the screw wings may be configured to move in the direction of the pyrolysis chamber 200 by a rail, and waste located on the screw wings can be moved into the pyrolysis chamber 200. To this end, additional components such as rails and motors that enable the screw blade to operate may be included.

The pyrolysis chamber 200 includes a shielding member 210 that blocks or opens the waste movement path connected to the input unit 100, a pyrolysis space 220 in which waste input through the input unit 100 is placed, and a pyrolysis space 220 in which waste introduced through the input unit 100 is placed, and a combustible fuel is disposed in the waste. It may include a fuel pump 230 that injects fuel, and an ignition unit 240 that generates a flame in the pyrolysis space 220.

Since thermal decomposition is carried out at a temperature of 200°C to 800°C under low oxygen conditions, the thermal decomposition space 220 must be kept sealed to prevent external air from entering. Therefore, the shielding member 210 remains open so that waste can be moved to the pyrolysis space 220, but when the movement of waste is completed, the waste movement path between the input unit 100 and the pyrolysis space 220 is closed. By blocking, the thermal decomposition space 220 is made sealed.

When thermal decomposition of waste proceeds in the pyrolysis space 220, combustion residue consisting of fuel gas and ash is generated, and the fuel gas is a flammable gas consisting of more than 70% hydrogen and is a toxic substance. The ash may remain in the form of solid carbide lumps and be discharged to the first discharge unit 400.

Garbage is combustible materials such as waste synthetic rubber, plastic packaging, waste synthetic polymer compounds, waste synthetic resin, waste tires, waste foamed synthetic resin, waste fishing nets, waste wood, SRF, and medical waste, and initial ignition is required for thermal decomposition.

The fuel pump discharges highly flammable liquid fuel, such as kerosene, into the pyrolysis space 220, and the ignition unit 240 may provide flame to the pyrolysis space 220 for a preset time for initial ignition of the waste. Since thermal decomposition begins when part or all of the trash is ignited, the ignition unit 240 may provide flame to the trash for a certain period of time, for example, about 5 minutes, and then block the flame.

Fuel gas is a complex gas composed of more than 70% hydrogen. Hydrogen is the lightest gas and has the property of diffusing quickly, and has a wider range of explosion limits than other hydrocarbon-based materials.

The gas supply pipe 250 can collect fuel gas in the pyrolysis space 220 and supply it to the ultra-high temperature gasification chamber 300. The gas supply pipe 250 may be formed with an injection nozzle 251 that injects fuel gas into the ultra-high temperature gasification space 350 and a hollow screw portion 252 for screw connection with the adjustment member 341.

The gas supply pipe 250 is disposed between the pyrolysis chamber 200 and the ultra-high temperature gasification chamber 300, and the fuel gas generated in the pyrolysis chamber 200 by the operation of sucking or blocking fuel gas is transferred to the ultra-high temperature gasification chamber 300. ) can be supplied or not supplied. In addition, the gas supply pipe 250 may include a hole through which fuel gas passes, and the amount of fuel gas supplied from the pyrolysis chamber 200 to the ultra-high temperature gasification chamber 300 can be adjusted by adjusting the size of the hole. .

The ultra-high temperature gasification chamber 300 supplies high-pressure gas to the fuel gas and can cause spontaneous ignition of hydrogen by causing a strong diffusion effect between the fuel gas and the high-pressure gas. Since the ultra-high temperature gasification chamber 300 completely decomposes combustion gas using spontaneous combustion, it does not require a separate ignition source for ignition.

For hydrogen to explode, the minimum energy required for ignition is required, and this energy is called the minimum ignition energy, and the minimum ignition energy for general hydrocarbons is about 0.24 mJ. In the case of hydrogen, the minimum ignition energy is 0.017 mJ at 101.3 kPa, which is an extremely small energy, and there is a possibility of ignition even with energy as small as a person's static electricity.

In addition, the minimum ignition energy of hydrogen is 0.56 mJ at 2.03 kPa, but changes to 0.09 mJ at 5.1 kPa, showing a tendency for the minimum ignition energy to decrease as the pressure decreases.

Therefore, the ultra-high temperature gasification chamber 300 injects high-pressure gas into the fuel gas, so that the shock wave compresses the hydrogen in the fuel gas, increasing the temperature of the hydrogen and increasing the possibility of ignition. Since the higher the blowing pressure of the high-pressure gas, the higher the possibility of self-ignition of hydrogen, the ultra-high temperature gasification chamber 300 can spontaneously ignite the fuel gas and control the ignition temperature by adjusting the blowing pressure of the high-pressure gas.

The ultra-high temperature gasification chamber 300 can control the flame temperature to an ultra-high temperature of 1400°C to 2000°C by controlling the ejection pressure of the high-pressure gas.

The second discharge unit 500 discharges the gas obtained by gasifying the fuel gas in the ultra-high temperature gasification chamber 300 to the outside, and the gasified gas is a gas in which pollutants have been completely decomposed, as shown in Table 1.

The compressor 600 provides high-pressure gas to the ultra-high temperature gasification chamber 300 through the high-pressure gas transfer pipe 610, and the high-pressure gas may be composed of high-pressure air, high-pressure oxygen, etc.

Figure 3 is a perspective view of an ultra-high temperature gasification chamber according to an embodiment of the present invention, Figure 4 is a cross-sectional view of an ultra-high temperature gasification chamber according to an embodiment of the present invention, and Figure 5 is an exploded perspective view of a flow rate control unit according to an embodiment of the present invention. .

Referring to FIGS. 3 to 5, the gas supply pipe 250 includes an injection nozzle 251 that injects fuel gas into the ultra-high temperature gasification space 350, and a hollow screw portion 252 for screw connection with the adjustment member 341. can be formed.

The ultra-high temperature gasification chamber 300 provides an ultra-high temperature gasification space 350 in which the fuel gas supplied from the injection nozzle 251 is spontaneously ignited by high-pressure gas and diffusion, and the high-pressure gas supplied from the compressor 600 is supplied. It includes a gas supply unit 310 and a flow rate controller 320 for controlling the supply amount of high-pressure gas.

The ultra-high temperature gasification chamber 300 is made of a tube body and includes first and second connecting members 311 and 321 that come into contact with each other to provide an ultra-high temperature gasification space 350, and the first and second connecting members 311 and 321 A coupling member 330 may be screwed to the inside of the connection end where 321) abuts each other.

An expanded flame guide pipe 340 is connected to the tip of the first connecting member 311, and the flame guide pipe 340 guides the direction of movement of the flame generated in the ultra-high temperature gasification space 350 and removes combustion residues. A path for this discharge can be provided.

The injection nozzle 251 of the gas supply pipe 250 may be disposed at the center of the rear end of the second connecting member 321. A plurality of ventilation holes 322 are formed in the rear end wall of the second connecting member 321, and a plate-shaped adjustment member 341 may be disposed on the outer side opposite to the ventilation hole 322. The amount of air flowing into the ventilation hole 322 can be adjusted by the gap between the second connecting member 321 and the adjusting member 341.

The adjusting member 341 is movable by screwing with the hollow screw portion 252 of the gas supply pipe 250, and a spring 342 is disposed at the inner end of the adjusting member 341. The spring 342 can elastically support the adjustment member 341 at a set position so that it does not arbitrarily move in the hollow screw portion 252.

A high-pressure gas inflow chamber 352 is formed inside the first connecting member 311 into which high-pressure gas flows, and on one side of the first connecting member 311, the high-pressure gas is supplied from the compressor 600 through the transfer pipe 610. A high-pressure gas inlet 313 may be formed to guide the provided high-pressure gas.

The high-pressure gas inlet chamber 352 is formed between the first connecting member 311 and the coupling member 330, so that the high-pressure gas introduced through the high-pressure gas inlet 313 can be supplied toward the air amplification induction path 351. It is formed so that

First and second inclined surfaces 312 and 332 forming an inclination angle are formed in front of the high-pressure gas inlet chamber 352, so that the high-pressure gas supplied to the high-pressure gas inlet 313 flows through the first and second inclined surfaces 312 and 332. 332) can be amplified and supplied to the ultra-high temperature gasification space 350 through the gap between them.

The first inclined surface 312 is formed on the inner peripheral surface of the first connecting member 311, and the second inclined surface 332 is formed on the outer peripheral surface of the coupling member 330, and the first and second inclined surfaces 312 and 332 are Formed at different inclination angles. Depending on the coupling position of the first connecting member 311 screwed to the coupling member 330, the gap between the air amplification induction passages 351 can be adjusted to widen or narrow.

Additionally, the tip of the second inclined surface 332 may be provided with an inclined inducing surface 331 and a right-angled cross-section 333 at an angle lower than the inclined line of the second inclined surface 332. The inclined guide surface 331 and the right-angled cross-section 333 are configured to generate negative pressure, and a strong suction force is generated in the direction of flame progression of the ultra-high temperature gasification chamber 300, resulting in strong diffusion between the amplified high-pressure gas and fuel gas. causes it to act.

As the high-pressure gas and fuel gas cause diffusion, when the high-pressure gas is ejected into the fuel gas, the shock wave compresses the fuel gas and mixes hydrogen at the contact surface. As the high-pressure gas and fuel gas are mixed, the temperature increases and the hydrogen in the fuel gas spontaneously ignites.

That is, after the high-pressure gas is introduced from the compressor 600 into the high-pressure gas inlet chamber 352, the high-pressure gas is amplified through the air amplification induction path 351 formed in front of the high-pressure gas inlet chamber 352 to provide fuel gas. If they collide, a strong diffusion effect may occur between the amplified high-pressure gas and the fuel gas, resulting in spontaneous combustion.

The higher the blowout pressure of the high-pressure gas, the stronger the shock wave is generated in the fuel gas, and the jet flow of hydrogen increases the temperature of the mixed gas and increases the ignition temperature.

The ultra-high temperature gasification chamber 300 adjusts the gap between the first and second inclined surfaces 312 and 332, adjusts the pressure of the high-pressure gas supplied from the compressor 600, or controls the second connection member 321 and the adjustment member. (341) The injection pressure of the high-pressure gas can be adjusted by adjusting the amount of air inflow.

For example, the ultra-high temperature gasification chamber 300 narrows the gap between the first and second inclined surfaces 312 and 332 in order to increase the blowing pressure of the high-pressure gas and increase the ignition temperature of the fuel gas, or It is possible to increase the pressure of the high-pressure gas or increase the amount of air inflow between the second connection member 320 and the control member 341.

In this way, the ultra-high temperature gasification chamber 300 according to an embodiment of the present invention can adjust the flame temperature between 1400°C and 2000°C by controlling the shock wave applied to the fuel gas by the amplified high-pressure gas by controlling the ejection pressure of the high-pressure gas. .

Above, embodiments of the present invention have been described with reference to the attached drawings, but those skilled in the art will understand that the present invention can be implemented in other specific forms without changing its technical idea or essential features. You will be able to understand it. Therefore, the embodiments described above should be understood in all respects as illustrative and not restrictive.

10: Complete waste decomposition and recycling device
100: Input part
200: Pyrolysis chamber
300: Ultra-high temperature gasification chamber
400: first discharge unit
500: second discharge unit
600: Compressor

Claims (10)

An input section where waste is input;
A pyrolysis chamber including a pyrolysis space for pyrolyzing input waste;
An ultra-high temperature gasification chamber that gasifies the fuel gas generated by thermal decomposition in the thermal decomposition space of the thermal decomposition chamber at ultra-high temperature; and
It includes a gas supply pipe that supplies fuel gas from the pyrolysis chamber to the ultra-high temperature gasification chamber,
The ultra-high temperature gasification chamber,
A first connecting member forming an ultra-high temperature gasification space;
a second connecting member provided in contact with the lower portion of the first connecting member and having a plurality of vent holes through which fuel gas generated in the pyrolysis space moves; and
A high-pressure gas supply unit connected to the first connection member and guiding the high-pressure gas provided from the compressor to the ultra-high temperature gasification space to generate spontaneous ignition by diffusion with the fuel gas,
The ultra-high temperature gasification chamber is a waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, characterized in that the second connecting member is connected to the pyrolysis chamber so that it is disposed on the pyrolysis space. The method of claim 1, wherein the input unit,
A conveyor unit transporting the waste input into the input unit to the pyrolysis chamber; and
A complete waste decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, further comprising a screw part extending from the conveyor part and rotating so that the waste can be supplied into the pyrolysis chamber. The method of claim 1, wherein the pyrolysis chamber is,
a fuel pump that discharges highly flammable liquid fuel into the pyrolysis space; and
A waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, including an ignition unit that provides a flame to the pyrolysis space. The method of claim 3, wherein the pyrolysis chamber is,
A waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, further comprising a shielding member that blocks or opens the waste movement path between the input unit and the pyrolysis chamber. According to paragraph 3,
The pyrolysis space is sealed from the outside to maintain low oxygen conditions during the pyrolysis period,
A waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, wherein the ignition unit provides the flame to the waste only during a preset time for initial ignition. According to paragraph 1,
a first discharge unit that discharges combustion residues generated after thermal decomposition in the thermal decomposition chamber to the outside; and
A waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, further comprising a second discharge unit for discharging combustion residues generated after combustion in the ultra-high temperature gasification chamber to the outside. The method of claim 1, wherein the ultra-high temperature gasification chamber,
A waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, including a spray nozzle disposed at the center of the rear end of the second connecting member and spraying the fuel gas into an ultra-high temperature gasification space. The method of claim 7, wherein the ultra-high temperature gasification chamber,
A waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, further comprising a flow rate control unit that controls the amount of air inflow into the ultra-high temperature gasification space by adjusting a plate-shaped control member disposed on the outside opposite the ventilation hole. The method of claim 7, wherein the high pressure gas supply unit,
a high-pressure gas inlet that introduces high-pressure gas provided from the compressor into one side of the first connecting member; and
A waste complete decomposition recycling treatment device using pyrolysis gasification for carbon neutrality, including a high-pressure gas inlet chamber that supplies the high-pressure gas introduced through the high-pressure gas inlet to the ultra-high temperature gasification space through an air amplification induction furnace. The method of claim 7, wherein the ultra-high temperature gasification chamber,
It is connected to the tip of the first connecting member, and further includes a flame guide tube that guides the direction of progress of the flame generated in the ultra-high temperature gasification space and provides a path through which combustion residues of the fuel gas are discharged. A waste recycling treatment device that completely decomposes waste using pyrolysis gasification.

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