KR20110026933A

KR20110026933A - A supplying apparatus for supplying waste combustible materials, apparatus for producing fuel oil by continual pyrolysis thereof

Info

Publication number: KR20110026933A
Application number: KR20090084793A
Authority: KR
Inventors: 현재호
Original assignee: 주식회사 케이디텍; 현재호
Priority date: 2009-09-09
Filing date: 2009-09-09
Publication date: 2011-03-16
Also published as: KR101243191B1

Abstract

Disclosed is an energy efficient eco-friendly flammable waste continuous pyrolysis emulsifier. The present invention transfers the crushed combustible waste pieces by a predetermined amount, and the raw material feed supply device for supplying the waste transferred to a predetermined amount in an oxygen-free or low-oxygen atmosphere state, a pyrolysis device, a plurality of thermal decomposition of the supplied waste in a continuous stable operating conditions A pyrolysis unit consisting of a combustion furnace for supplying a heat source using oil and non-condensable gas as fuel in the pyrolysis chambers and the pyrolysis chambers, a reforming tower for removing foreign substances from the pyrolyzed pyrolysis gas, and a reformed gas for the reforming tower. It is composed of a pyrolysis gas condensing device composed of condensing means for producing and storing high quality oil, and a residue discharging device for automatically and safely discharging the remaining residue after disconnection from external air. Therefore, the present invention continuously supply the crushed combustible waste pieces continuously in the pyrolysis chamber under anoxic or low oxygen atmosphere conditions, and produce pyrolyzed pyrolysis gas as a high quality mixed refined oil, non-liquefied non-liquefied By using the condensation gas as a heat source for pyrolysis, it provides an effect that can be expected energy-efficient eco-friendly flammable waste pyrolysis emulsification equipment.

Description

A supplying apparatus for supplying combustible waste and a pyrolysis emulsifying apparatus for continuous pyrolysis thereof {A supplying apparatus for supplying waste combustible materials, apparatus for producing fuel oil by continual pyrolysis

The present invention relates to the recycling of flammable waste such as rubber, waste synthetic resins, waste plastics, and more particularly, by supplying flammable waste continuously in a state in which the outside air is blocked to be completely pyrolyzed to produce high quality refined oil. In addition, the present invention relates to a supply device for supplying flammable waste in which residual gas is used as a pyrolysis heat source, and a pyrolysis emulsification device for continuous pyrolysis thereof.

In general, in the field of waste treatment, the liquor of the prior art is mostly incinerated with air, but recovers the heat of incineration generated as much as possible, removes the harmful substances contained in the combustion gas below the legal limit, and then removes a large amount of the combustion gas. At the same time as the discharge to the atmosphere, a series of treatments are performed to solidify the landfill by burning the residue and fly ash generated.

However, the secondary pollution due to the accumulation of harmful substances remaining in the combustion gas discharged to the atmosphere during the waste treatment process and the residual harmful substances solidified and buried, as a factor of serious environmental degradation, the development of new waste treatment technology is required. It is becoming.

In order to meet such a demand, the development of the technology which can recycle a waste in recent years is actively going on.

For example, a method of recycling polymer wastes such as waste plastics made from petroleum as a raw material of flammable wastes, which decomposes a polymer material by applying heat in an oxygen-free condition and converts it into a low-molecular material to return it to oil. Pyrolysis emulsion technology.

Existing flammable waste pyrolysis emulsifying apparatus has two methods: a batch type in which waste is charged into a pyrolysis chamber to apply heat from the outside, and a continuous type of pyrolysis while continuously injecting waste into the pyrolysis chamber.

In the pyrolysis chamber having a narrow volume, all of them heat the heat required for pyrolysis in a short time. As a result, carbon is coated on the wall of the pyrolysis chamber, resulting in rapid heat transfer and poor thermal decomposition. In addition, various problems such as the various facilities of the pyrolysis chamber did not operate smoothly due to rapid feed heating.

In addition, in the discharge of residues generated after pyrolysis, there are many problems in discharging the residues automatically and safely in a state of being blocked with external air.

For this reason, although many pyrolysis apparatuses have been developed, they are not practically used in the industrial field.

Accordingly, an object of the present invention has been made in view of the above-mentioned point, and to provide a supply apparatus for supplying crushed combustible waste pieces while maintaining an anoxic or low oxygen atmosphere so as to increase the thermal decomposition efficiency of combustible waste. .

It is also an object of the present invention to maximize the contact area with the heat source required for pyrolysis of the combustible waste continuously supplied from the supply device for supplying the above-mentioned combustible waste, so that complete pyrolysis is achieved, and the gas generated by pyrolysis is improved. And it provides a combustible waste continuous pyrolysis emulsification apparatus that can be condensed to produce a high quality mixed refined oil.

It is also an object of the present invention to provide a flammable waste continuous pyrolysis emulsification apparatus having safety and efficiency of continuous operation by automatically discharging the remaining residue after the completion of pyrolysis in a state disconnected from external air.

The supply device for supplying the combustible waste of the present invention for achieving the above object is, in the apparatus for supplying combustible waste to the pyrolysis chamber of the pyrolysis emulsification apparatus of the combustible waste, raw material for transferring the crushed combustible waste pieces by a predetermined amount It is equipped with a transfer means and a plurality of gates that can be opened and closed, and automatically supplies the waste transferred to the pyrolysis chamber in a certain amount in an oxygen-free or low-oxygen atmosphere by blocking the inflow of external air by repeatedly opening and closing the connected multiple gates. Contains input means.

The combustible waste continuous pyrolysis emulsifying apparatus for achieving the object of the present invention, in the pyrolysis emulsifying apparatus for pyrolyzing combustible waste to produce oil, transfer the crushed combustible waste pieces by a predetermined amount, and the waste to be transported in a certain amount without oxygen A supply device that continuously supplies while maintaining a low oxygen atmosphere, a plurality of pyrolysis chambers that pyrolyze the combustible waste pieces continuously under stable operating conditions, and a combustion source that supplies oil and non-condensable gas as fuel to the pyrolysis chambers as fuel. A pyrolysis device consisting of a furnace, a residue discharge device for automatically discharging the residue left after pyrolysis in the state of being disconnected from external air, a reforming tower for reforming pyrolysis gas, and a plurality of condensers for condensing the reforming gas to produce oil. And a pyrolysis gas condensation device.

The supply apparatus for supplying the combustible waste of the present invention and the pyrolysis emulsifying apparatus for continuous pyrolysis thereof, have two or more stages of pyrolysis chambers having a large volume and area regardless of the shape of the combustible waste that is crushed and supplied during continuous pyrolysis of the combustible waste. In order to maximize the contact area with the heat source required for pyrolysis, complete pyrolysis is achieved, and the remaining residues are kept in a dry state and discharged automatically by the continuous automatic discharge device that is essential for continuous operation. In addition, the gas generated by pyrolysis is passed through the filtering device to remove internal foreign substances and reformed in a metal catalyst reforming tower to produce high quality mixed refined oil.

In addition, thermal decomposition can be performed regardless of the shape and density of materials such as waste synthetic resin, waste vinyl, composite waste vinyl, and waste rubber, and energy-efficient and environmentally-friendly pyrolysis using non-condensable gas as a heat source for pyrolysis facilities. By providing emulsification technology, it is possible to increase the recycling of flammable waste, which has the effect that can be put to practical use in many industrial sites in the future.

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

1 is an overall configuration diagram schematically showing a flammable waste continuous pyrolysis emulsion apparatus according to the present invention.

The pyrolysis emulsifying apparatus shown in FIG. 1 is largely composed of a supply apparatus 100 for supplying flammable waste, a pyrolysis apparatus 200, a residue discharging apparatus 300, and a pyrolysis gas condensing apparatus 400.

The supply device 100 is a raw material conveying means 110 for transferring the shredded combustible waste pieces by a predetermined amount, and an automatic input means for supplying the waste conveyed in a predetermined amount to the pyrolysis apparatus 200 while maintaining an oxygen-free or low-oxygen atmosphere state ( 120). A detailed configuration of the supply device 100 will be described later with reference to FIGS. 2A and 2B.

The pyrolysis apparatus 200 is a heat source using two stages of pyrolysis chambers 210 and 220 having a large volume and area for pyrolyzing the supplied wastes under continuous and stable operating conditions, and oil and non-condensable gas as fuels in the pyrolysis chambers 210 and 220. It consists of a combustion furnace 230 for supplying. In the present embodiment, the pyrolysis chamber is configured in two stages of primary and secondary, but the pyrolysis chamber may be configured in two or more stages. A detailed configuration of the pyrolysis device 200 will be described later with reference to FIGS. 3A to 3C.

Residue discharge device 300 is composed of a cooling means 310 for cooling the high temperature residue remaining after the completion of pyrolysis, and the discharge means 320 for automatically discharging the residue in a state disconnected from the external air. A detailed configuration of the residue discharge device 300 will be described later with reference to FIGS. 4A and 4B.

The pyrolysis gas condensing apparatus 400 includes a reforming tower 410 for removing foreign substances and reforming the pyrolyzed pyrolysis gas, a condensation means 420 for producing the reformed gas as a high quality oil, and storing the produced oil. The storage means 430 is made. A detailed configuration of the pyrolysis gas condensing device 400 will be described later with reference to FIGS. 5A and 5B.

The pyrolysis emulsification operation of producing oil by continuously supplying flammable waste in the apparatus of FIG. 1 having such a configuration will be described in detail.

After combustible waste such as rubber, waste synthetic resin, plastic waste, etc. are crushed in a crusher (not shown), the crushed combustible waste pieces are put into the supply device 100.

Figure 2a is a detailed view showing the supply device 100 of Figure 1, Figure 2b shows a connection state diagram of the automatic injection means 120 and the pyrolysis device 100 in Figure 2a.

Referring to FIG. 2A, the raw material conveying means 110 has a space 113 formed by removing a wing in a middle portion of the conveying screw 112 and the conveying screw 112 configured in the case 111. The case 111 is inclined at a predetermined angle with respect to the horizontal plane so that the conveyance of waste is directed upward. The end of the case 111 has a drive motor 114 connected to the rotating shaft of the transfer screw 112.

When crushed combustible waste pieces such as waste plastic are supplied, the drive motor 114 is operated to rotate the transfer screw 112 at a constant speed. As the transfer screw 112 rotates, wastes are transferred in the case 111. At this time, the waste pieces conveyed by the space 113 formed in the middle of the inside of the case 111 of the raw material conveying means 110 are stacked and transferred. That is, the waste pieces are accumulated in the inner space during the transfer, and the primary pieces are blocked by the external air and then transferred to the automatic feeding means 120.

The automatic feeding means 120 has openable gates 121 to 123 mounted in multiple stages. In this embodiment, the closed gates were configured in three stages. When the waste is transported from the raw material transfer means 110, firstly, the primary sealing gate 121 mounted at the top is opened and the waste pieces are introduced into the secondary sealing gate 122. At this time, the secondary hermetic gate 122 is in a closed state. Then, after closing the primary sealing gate 121 to make a sealed state, the secondary sealing gate 122 is opened to inject waste pieces into the tertiary sealing gate 123. At this time, the tertiary sealed gate 123 is in a closed state. Then, the secondary sealing gate 122 is also closed to make the sealed state to block the inflow of air from the outside. The primary and secondary sealed gates 121 and 122 are closed to maintain an anoxic or low oxygen atmosphere in which external air is blocked, and the tertiary sealed gate 123 is opened to open the waste pieces as shown in FIG. 2B. ) Automatically put into the inside.

As described above, the opening, closing and closing of the primary, secondary and tertiary sealed gates 121 to 123 are repeatedly operated to supply waste pieces to the pyrolysis apparatus 200 continuously while blocking external air inflow as much as possible to perform continuous pyrolysis operation. Make it possible.

3A is a detailed view illustrating a pyrolysis apparatus 200 of the apparatus of FIG. 1, FIG. 3B is a view showing exhaust gas emissions of the pyrolysis chambers 210 and 220, and FIG. 3C is a diagram showing a pyrolysis process inside the pyrolysis chambers 210 and 220. to be.

3A, the pyrolysis apparatus 200 has a two-stage structure in which a primary pyrolysis chamber 210 is connected to an automatic input means 120, and a secondary pyrolysis chamber 220 is connected to a primary pyrolysis chamber 210. It is. The configurations of the primary pyrolysis chamber 210 and the secondary pyrolysis chamber 220 are the same. However, the secondary pyrolysis chamber 220 is combined with the residue discharge device 300 so that the foreign substances and residues remaining after pyrolysis are discharged. In the first pyrolysis chamber 210 and the second pyrolysis chamber 220, as shown in FIG. 3b, heating jackets 211 and 221 are installed around the cylinder, and the hot air generated in the combustion furnace 230 is supplied therein. The receiving heat supply tubes 212 and 222 and a plurality of transfer screws 213 to 215 and 223 to 225 are installed. The feed screws 213 to 215, 223 to 225 are rotated by the drive motors 216 to 218, 226 to 228.

Waste pieces automatically introduced from the tertiary closed gate 123 of the automatic input means 120 are pyrolyzed in the primary pyrolysis chamber 210 of the pyrolysis apparatus 200 to which the waste pieces are connected. The heat source required for pyrolysis in the primary pyrolysis chamber 210 uses hot air generated in the combustion furnace 230 as an indirect heat source. The hot air generated from the combustion furnace 230 is supplied into the pyrolysis chambers 210 and 220 through the heat supply tubes 212 and 222, and the hot air is supplied to the outside of the pyrolysis chambers 210 and 220 through the heating jackets 211 and 221 to thermally decompose the waste heat. The required heat is thermally decomposed by adding the heat to the pyrolysis chambers 210 and 220 as a whole. As the fuel required for the combustion furnace 230, the hot air is supplied to the pyrolysis chambers 210 and 220 by using gas oil at the start of the initial operation, and when the pyrolysis gas is generated by pyrolysis, the pyrolysis gas condensing unit 400 supplies the pyrolysis gas. After condensation, mixed refined oil is produced and the remaining non-condensed gas is fed back and used as the main fuel source. The hot air supplied from the combustion furnace 230 is used in the pyrolysis chambers 210 and 220 and then sent to the chimney through the exhaust duct 240 as shown in FIG. 3B.

The waste pieces put into the primary pyrolysis chamber 210 are decomposed with a large volume and an area, as shown in FIG. 3C, under an oxygen-free or low oxygen atmosphere condition in the main body, and with an optimum heat supply by a heat supply tube and a heating jacket. The mixture is melted and mixed by the screws 213 to 215 at a temperature of 320 to 420 ° C. under a pressure of ± 0 mmAg, and transferred to the secondary pyrolysis chamber 220 to pyrolyze in an optimal pyrolytic reducing atmosphere.

The non-pyrolyzed melt introduced into the secondary pyrolysis chamber 220 is completely pyrolyzed in the secondary pyrolysis chamber 220, and only the residues remaining after the pyrolysis is discharged to the residue discharge device 300. The heat source required for pyrolysis of the secondary pyrolysis chamber 220 receives hot air from the combustion furnace 230 through the heat supply tube 222 and the heating jacket 221 like the primary pyrolysis chamber 210.

The pyrolysis gas pyrolyzed in the first and second pyrolysis chambers 210 and 220 is discharged to the condenser 400 through the gas discharge pipe 250.

4A and 4B are detailed and side views showing the residue discharge device 300 of the device of FIG. 1.

Referring to Figure 4a, the residue discharge device 300 is coupled to the outlet of the secondary pyrolysis chamber 220, the cooling means 310 for cooling the high temperature residue from the outlet and the cooling means 310 It is composed of a discharge means 320 for discharging the discharged residue to the outside.

As shown in FIG. 4A, the cooling means 310 is provided with a screw 311 capable of receiving and transporting a high temperature residue from the outlet of the pyrolysis apparatus 200, and allowing the cooling water to pass through to prevent overheating. The cooling jacket 312 is provided. The screw 311 is rotated by the drive motor 313. The cooling jacket 312 is connected with a cooling tower 330 for circulating and supplying cooling water.

Pyrolysis is performed through the first and second pyrolysis chambers 210 and 220 in turn, and the remaining high-temperature residue is discharged to the cooling means 310 through the outlet. The cooling means 310 operates the driving motor 313 to rotate the screw 311 to transfer the high temperature residues from the outlet to the discharge means 320. At this time, the cooling water is circulated and supplied to the cooling jacket 320 through the cooling tower 330 to cool the high temperature residue. Cooled residue is transferred to the discharge means (320).

Discharge means 320 is a plurality of discharge pipes (321,322) commonly connected to the cooling means 310, as shown in Figure 4b, the separation gate to the common connection to alternately distribute the residue to the plurality of discharge pipes (321,322) 323 is provided. The plurality of discharge pipes 321 and 322 have the same configuration. Inside the discharge pipes 321 and 322, the opening and closing gates 321A and 322A installed at the inlet side, the hoppers 321B and 322B, the discharge screws 321C and 322C, and the opening and closing gates 321D and 322D provided at the outlet side. Has Screws 321C and 322C are also rotated by the drive motors 324 and 325.

When the residue to be discharged from the cooling means 310 is transported, the secondary discharge pipe 322 is blocked by the separation gate 323 so that all the residue flows into the primary discharge pipe 321. In the primary discharge pipe 321, the inlet side gate 321A is opened to allow the residue to be stored in the hopper 321B. At this time, the exit gate 321D is kept closed. When the residue is loaded in the hopper 321B by a predetermined reference value, the primary discharge pipe 321 is blocked by the separation gate 323 so that all the residue flows into the secondary discharge pipe 322. In the secondary discharge pipe 322, the inlet side gate 322A is opened to allow the residue to be stored in the hopper 322B. While the residues are stored in the hopper 322B of the secondary discharge pipe 322, the inlet gate 321A of the primary discharge pipe 321 is closed and the outlet gate 321D is opened to completely block external air. By operating the discharge screw (321C) in the state to discharge the residue loaded on the hopper (321B) to the outside.

While the residues loaded into the hopper 321B of the primary discharge pipe 321 are discharged, the residues are loaded into the hopper 322B of the secondary discharge pipe 322, and at this time, the exit gate 322D is closed. The external air is completely blocked so that no air enters the primary and secondary combustion chambers 210 and 220, so that the continuous pyrolysis operation can be safely performed.

Meanwhile, the high temperature pyrolysis gas discharged from the first and second pyrolysis chambers 210 and 220 is discharged to the condenser 400 through the pyrolysis gas discharge pipe 250 as shown in FIG. 3A.

5A is a detailed view illustrating the condenser 400 of the apparatus of FIG. 1, and FIG. 5B is a configuration diagram illustrating the interior of the reforming tower 410 of FIG. 5A.

Referring to FIG. 5A, the condenser 400 is connected to the reforming tower 410 to the gas discharge pipe 250 of the pyrolysis apparatus 200. The gas reforming tower 410 is composed of catalyst layers 411 and 412 installed in the middle of the interior to promote pyrolysis. The gas reforming tower 410 is provided with condensing means 420 including a plurality of condensers 421 to 423 for condensing the reformed gas discharged from the reforming tower 410 to produce refined oil.

The pyrolysis gas is transferred to the reforming tower 410 through a transfer pipe 440 connected to the gas discharge pipe 250 of the pyrolysis device 200. The gas reforming tower 410 primarily filters the pyrolysis gas to remove foreign substances in the gas, ie, soil, carbon heavy oil, and the like, and transfers the decomposed gas to the primary pyrolysis chamber 210. The pyrolyzed gas passes through the primary metal catalyst layer 411 and the secondary metal catalyst layer 412 mounted on the reforming tower 410 to reform the paraffin chain longer than C _{25 in} the pyrolysis gas. Here, as the metal catalyst, nickel (Ni), copper (Cu), lead (Pb), chromium salt (Cr ₃ ), or the like, ceramics and synthetic zeolites are used. The reformed gas is condensed in the primary and secondary condensers 421 and 422 through the transfer pipe 450 to produce light oil grade refined refined oil, and the tertiary condenser 423 produces kerosene grade refined oil. At this time, the pyrolysis gas produced in the pyrolysis chambers 210 and 220 by the operation of the gas blowers 424 and 425B is transferred to the condenser 400 along the gas pipe, and is produced by the condensers 421 to 423 of the condenser 400. The mixed refined oil is separated into oil and water in the collection tanks 421A to 423A specified in FIG. 5A, and then stored in the storage means 430. At this time, the cooling water required by the condensers 421 to 423 is circulated and supplied from the cooling tower 330.

As described above, the remaining non-condensable gas is passed through the non-condensable gas stabilization tank 460 to the combustion furnace 230 in a state in which it is blocked from the outside air in the sealing tank 470 to be pyrolysis chambers 210 and 220. Will be used as the primary fuel.

6A and 6B illustrate the overall detailed configuration diagram of the apparatus of FIG. 1, and each configuration has been described above.

As described above, the pyrolysis emulsifying apparatus of the present invention can increase the energy consumption efficiency according to the operation of the equipment for producing oil by supplementing and operating the gas produced by itself after consuming the energy required for the first operation.

1 is a block diagram showing a flammable waste continuous pyrolysis emulsion apparatus according to the present invention,

2A-2B are detailed views of the supply apparatus of the apparatus of FIG. 1;

3A-3C are detailed views of the pyrolysis apparatus of the apparatus of FIG. 1;

4a-4b is a detailed view showing the residue discharge device of the device of Figure 1,

5A-5B are detailed views showing the pyrolysis gas condenser of the apparatus of FIG. 1;

6A-6B are detailed configuration diagrams corresponding to the FIG. 1 apparatus.

100: supply device 110: raw material transfer means

120: automatic injection means 200: pyrolysis device

210,220 pyrolysis chamber 230 combustion furnace

240: exhaust duct 250: gas discharge pipe

300: residue discharge device 310: cooling means

320: discharge means 400: pyrolysis gas condenser

410: reforming tower 420: condensation means

430: storage means

Claims

An apparatus for supplying flammable waste to a pyrolysis chamber of a pyrolysis emulsifying apparatus of flammable waste,

Raw material transfer means for transferring the shredded combustible waste pieces by a predetermined amount; And

It is equipped with a plurality of gates that can be opened and closed, the automatic input means for supplying waste to the pyrolysis chamber in a certain amount in an oxygen-free or low-oxygen atmosphere state by blocking the inflow of external air by repeatedly opening and closing the plurality of gates connected to the mounted gate. Feeder.

The method of claim 1, wherein the raw material conveying means

A screw configured to convey the shredded combustible waste piece by a rotational motion; And

It is provided with a drive motor for operating the screw at a constant speed,

Feeding device characterized in that to remove the wing in the middle of the screw to form a space, the waste transported in accordance with the rotation of the screw accumulated in the formed space to block the outside air and then transfer the waste to the automatic feeding means .

The method of claim 1, wherein the automatic input means is to open the primary sealed gate of the plurality of gates installed to transfer the waste pieces to the secondary sealed gate, and close the primary sealed gate to block the outside air inflow and secondary sealing Supplying the waste piece to the pyrolysis chamber by opening the gate to transfer the waste piece to the tertiary sealed gate, closing the secondary sealed gate to block external air inflow, and then opening the tertiary sealed gate.

In the pyrolysis emulsifying apparatus for producing oil by pyrolyzing flammable waste,

A supply device for transferring the crushed combustible waste pieces by a predetermined amount, and continuously supplying the waste to be transported in a predetermined amount in an oxygen-free or low-oxygen atmosphere;

A pyrolysis apparatus comprising a plurality of pyrolysis chambers for continuously decomposing the combustible waste pieces to be supplied under stable operating conditions, and a combustion furnace for supplying a heat source using oil and non-condensable gas as fuels to the pyrolysis chamber;

Residual discharge device for automatically discharging the remaining residue after the thermal decomposition is disconnected from the outside air; And

A combustible waste continuous pyrolysis emulsifying apparatus comprising a pyrolysis gas condensing device comprising a reforming tower reforming pyrolysis gas and a plurality of condensers condensing the reforming gas to produce oil.

The apparatus of claim 4, wherein the supply device is

Raw material transfer means for transferring the crushed combustible waste pieces by the rotational operation of the screw, forming a space so that the waste accumulates in the space and blocking the outside air so that the waste is transferred; And

A gate that can be opened and closed is mounted in multiple stages, and the gates connected to the pyrolysis apparatus in a state in which a space between the gates is sealed by receiving pieces of combustible waste transferred from the raw material transfer means by repeatedly opening and closing the connected gates repeatedly. Combustible waste continuous pyrolysis emulsifying device characterized in that it comprises an automatic input means for inputting the supplied combustible waste pieces to the pyrolysis device.

The method of claim 4, wherein the pyrolysis device

A primary pyrolysis chamber for mixing and melting pieces of combustible waste which are supplied and connected to the supply device to pyrolyze the pieces;

A second pyrolysis chamber connected to the first pyrolysis chamber to pyrolyze the pyrolyzed melt in the first pyrolysis chamber; And

After using the fuel required for the initial operation, using a non-condensing gas remaining in the pyrolysis gas condensing unit as a fuel to provide a combustion furnace for supplying hot air to the primary and secondary pyrolysis chamber, characterized in that the continuous pyrolysis of flammable waste Emulsifier.

The method of claim 6, wherein the primary and secondary pyrolysis chamber is

Heating jacket installed outside to apply heat from the outside;

A heat supply tube receiving heat from the combustion furnace and applying heat therein;

A plurality of screws for mixing the pieces of combustible waste supplied by the rotating operation, and conveying the melt of the combustible waste melted by heat supplied by the heating jacket and the heat supply tube;

A drive motor for rotating the screws; And

Combustible waste continuous pyrolysis emulsifying apparatus characterized by consisting of exhaust duct for discharging the exhaust gas to the chimney.

The method of claim 6, wherein the residue discharge device

Cooling means coupled to the outlet of the secondary pyrolysis chamber to cool the discharged high temperature residues; And

Combustible waste continuous pyrolysis emulsion apparatus characterized in that it comprises a discharge means for automatically discharging the residue via the cooling means to the outside in a state disconnected from the external air.

The method of claim 8, wherein the cooling means

Installed around the cooling jacket to circulate the coolant from the outside;

A screw transferring the residue cooled by the cooling water circulated by the cooling jacket by a rotation operation;

A drive motor for rotating the screw; And

Combustible waste continuous pyrolysis emulsion apparatus, characterized in that consisting of a cooling tower for circulating supply of cooling water to the cooling jacket.

The method of claim 8, wherein the discharge means

A plurality of discharge pipes commonly connected to the cooling means; And

It is provided in a portion where the plurality of discharge pipes are commonly connected, consisting of a separation gate for alternately distributing the residues transferred from the cooling means to the plurality of discharge pipes,

The plurality of discharge pipes

A gate capable of opening and closing at each of the inner inlet and outlet sides;

A hopper for storing residues supplied through the inlet gate;

A screw for discharging the residue stored in the hopper through the exit gate by a rotation operation; And

Combustible waste continuous pyrolysis emulsion apparatus, characterized in that consisting of a drive motor for rotating the screw.

The method according to claim 10, wherein the discharge means is configured to allow the residue to flow into the secondary discharge pipe by the separation gate when the residue is loaded in a hopper configured in the primary discharge pipe among the plurality of discharge pipes by a predetermined reference value. While the residue is stored in the hopper, the inlet gate of the primary outlet pipe is closed and the outlet gate is opened to discharge the residue in a state in which external air is blocked from entering the pyrolysis chamber along the pipe. Device.

5. The combustible waste continuous pyrolysis emulsifying apparatus according to claim 4, wherein the reforming tower of the pyrolysis gas condenser has a metal catalyst layer for reforming the gas pyrolyzed in the pyrolysis apparatus.

13. The combustible waste continuous pyrolysis emulsifying apparatus according to claim 12, wherein the metal catalyst layer uses nickel (Ni), copper (Cu), lead (Pb), chromium salt (Cr ₃ ), ceramics, and synthetic zeolites as catalysts. .