KR101337495B1 - Pyrolysis apparatus for solid-state combustible materials - Google Patents

Abstract

The present invention relates to a pyrolysis apparatus for a solid-state combustible material capable of reducing the emissions of pollutants and improving yield by indirectly heating and pyrolyzing a solid-state combustible material in a high-temperature not containing oxygen or containing oxygen. For the purpose, the present invention comprises a body of a pyrolyzer (210) including a main hopper for receiving a solid-state combustible material, including a pyrolysis screw (220) for transferring, melting and vaporizing the received combustible material, having a first body (211), a second body (213) and a third body (215) expanding on different levels, and transferring the combustible material with the second body (213) included to be able to rotate by using the difference in rotation rates from the pyrolysis screw; a pyrolysis room (240) installed outside the body of a pyrolyzer (20) to continuously pyrolyze the combustible material by an indirect heating method keeping a high-temperature atmosphere containing low oxygen; and a combustion room (250) placed at a side of the pyrolysis room (240) and supplying heat to the pyrolysis room (240) by combusting non-condensed gas among pyrolysis gas being generated in the pyrolysis of the combustible material to be used as a heat source for pyrolyzing the combustible material being transferred to the body of a pyrolyzer (210). [Reference numerals] (700) Gas purifying tool;(800) Refined oil generating tool;(900) Charcoal molding tool

Description

Pyrolysis apparatus for solid-state combustible materials}

The present invention relates to a pyrolysis device of a flammable material present in the solid phase, and more particularly, to induce heat decomposition of a flammable material in a solid state indirectly under a high temperature, anoxic or low oxygen atmosphere to reduce the emission of pollutants and improve the yield. The present invention relates to a pyrolysis apparatus for combustible materials in a solid state.

In general, the use of energy is rapidly increasing due to the increase of factories due to industrial development, and technology for converting the form of energy by recycling or reusing energy is being developed. In accordance with the requirements of the user, the initial energy resources in nature (for example, combustible crude oil, coal, wood, etc.) are being developed, and inorganic materials are processed from minerals which are not combustible materials. It is used in activities.

Among them, the combustible material has its own energy value because the calorific value varies depending on the element composition of the material (carbon, hydrogen, oxygen, nitrogen, sulfur, phosphorus, chlorine, etc.). If we use it around us and throw it away, it is called waste.

With the progress of industrialization, various kinds of metal debris, plastics, paper, and industrial wastes, which are used and discarded, have increased dramatically. Among them, combustible materials are burned by incinerator, which is a social problem due to environmental pollution. It is becoming. However, this method of incineration of combustible materials is a reality against the policy of reducing CO2 around the world.

In addition, since the processing costs and space limitations required for incineration of flammable materials are faced, most of the wastes are landfilled or illegally disposed. In addition, coal, which is a fossil fuel, emits a large amount of harmful substances such as carbon monoxide, carbon dioxide, and sulfurous acid gas by directly burning. As such, there is a problem that air, soil, and groundwater are seriously polluted due to pollution emission material and leachate generated during incineration and landfill of solid combustible materials.

A pyrolysis device is applied to treat such solid combustible materials. In the conventional pyrolysis device, a predetermined amount of waste is introduced into a pyrolysis chamber in a batch manner, and a lid is closed to remove high temperature heat from the outside. When the pyrolysis chamber is heated to a predetermined temperature, a batch method is adopted in which the waste is pyrolyzed and converted into liquid, gas and solid materials.

However, the batch type pyrolysis method has a lot of difficulties in pyrolysis of wastes in which various substances are mixed, and especially when foreign substances (such as grass, soil, ferrous and nonferrous metals) are mixed, heat transfer is not performed smoothly. Large scale pyrolysis is not achieved. In addition, there is a limit to the production of pyrolysis gas and refined oil in the mixed combustible and non-combustible material has a problem that the use value is lowered.

The present invention is to solve the problems as described above, in the case of pyrolyzing a solid combustible material in a high temperature, oxygen-free or low oxygen atmosphere by indirect heat, it is possible to process a large amount of solid combustible material in a small space It is an object to provide a pyrolysis device.

Another object of the present invention is to provide a pyrolysis apparatus capable of sufficiently removing foreign substances such as chlorine and sulfur contained in pyrolysis gas generated after pyrolysis to increase the purity of oil or gas extracted after pyrolysis.

The present invention is to solve the problems as described above, having a main hopper to which the solid combustible material is injected, the pyrolysis screw 220 for transporting, melting and vaporizing the injected combustible material is provided, the transport direction of the combustible material The first body 211, the second body 213, and the third body 215 is formed to be stepwise extended along the second body 213, the second body 213 is provided to be rotatable rotational speed with the pyrolysis screw A pyrolyzer body 210 for transporting the combustible material by the difference; A pyrolysis chamber 240 installed outside the pyrolyzer body 210 to continuously decompose the combustible material by indirect heating by maintaining an atmosphere of high temperature and low oxygen state; In addition, the pyrolysis chamber is provided on one side of the pyrolysis chamber 240 to burn the non-condensing gas of pyrolysis gas generated during pyrolysis of the combustible material so as to be used as a heat source for pyrolyzing the combustible material transferred to the pyrolyzer body 210. Technical features include a combustion chamber 250 that supplies heat to 240.

In addition, a sealing unit may be provided between the first body 211 and the second body 213, and between the second body 213 and the third body 215, respectively.

And the inlet portion of the third body 215 is formed in a circular shape so that no gap is formed with the pyrolysis screw, the middle portion of the third body 215 is formed in a streamline so that a predetermined space is formed with the pyrolysis screw. The rear end of the third body 215 may be formed in a circular shape such that a gap is not formed with the pyrolysis screw.

And it is preferable that the discharge hole 223 is formed in the screw blades of the pyrolysis screw provided in the second body 213 and the third body 215 section.

In addition, the gas retention tower 510 may be provided above the middle portion of the third body 215 of the pyrolysis body to retain the pyrolysis gas generated during pyrolysis of the combustible material for a predetermined time.

In addition, it is preferable that a spiral screw 520 is provided inside the gas retention tower 510 to separate tar and carbonized material attached to the inner wall of the gas retention tower.

And one side of the gas retention tower is preferably provided with a desalination device for removing chlorine in the pyrolysis gas.

And it is preferable to further include a gas purification means 700 for purifying the pyrolysis gas from which chlorine is removed from the desalination apparatus.

Further, it is preferable to further include refined oil producing means 800 for generating gasoline, light oil and heavy oil according to boiling points in the distillation column after sedimentation and condensation of pyrolysis gas from which chlorine is removed from the dechlorination reaction tower.

And it is preferable to further include a carbonized material discharge means for continuously discharging the carbonized material generated after pyrolysis from the pyrolysis chamber 240.

According to the present invention as described above, a portion of the pyrolyzer body 210 is rotated together with the pyrolysis screw 220 to maximize the heat providing area during pyrolysis to pyrolyze a large amount of solid combustible material in a small space. It has an effect that can be done.

In addition, since the desalination removal apparatus is provided in duplicate, the amount of chlorine removal in the pyrolysis gas can be minimized, thereby increasing the purity of oil or gas extracted after pyrolysis of the combustible material.

BRIEF DESCRIPTION OF THE DRAWINGS The accompanying drawings, which are incorporated in and constitute a part of the specification, illustrate preferred embodiments of the invention and, together with the description, serve to further the understanding of the technical idea of the invention, It should not be construed as limited.
1 is a block diagram showing the configuration of a pyrolysis apparatus for a solid combustible material according to an embodiment of the present invention,
Figure 2 is a partial perspective view showing the "X", "Y" display portion of FIG.
3 is a cross-sectional view illustrating lines AA, BB, CC, DD, EE, FF, and GG of FIG. 1;
4 is a partially enlarged view illustrating a display portion “Z” of FIG. 1;
FIG. 5 is a partially enlarged view showing a “W” display unit of FIG. 1;
Figure 6 is a schematic block diagram showing a refined oil production process according to an embodiment of the present invention.

Hereinafter, a preferred embodiment of the present invention will be described with reference to the drawings. In addition, the embodiment described below does not unduly limit the content of the present invention described in the claims, and the entire structure described in this embodiment is not necessarily essential as the solution means of the present invention.

1 is a block diagram schematically showing the configuration of a pyrolysis apparatus for a solid combustible material according to an embodiment of the present invention.

As shown in the drawings, the pyrolysis apparatus for a solid combustible material according to an embodiment of the present invention, a pyrolysis means for heating and thermally decomposing the combustible combustible material, a gas for removing chlorine from the pyrolysis gas generated during pyrolysis of the combustible material And reforming means, refining oil producing means for producing refined oil using the reformed gas, and carbonaceous material discharge means for continuously discharging carbonized material (char) discharged after pyrolysis from the pyrolysis means.

The pyrolysis principle used in the pyrolysis system of the present embodiment configured as described above is that when a solid combustible material is indirectly heated in an oxygen-free or low oxygen atmosphere, the pyrolysis space is formed in a reducing atmosphere, and the combustible material is decomposed to evaporate into a gas or a liquid. What does not remain solid.

That is, it can be seen that the combustible material (meaning a flammable polymer compound) + heat = gas (non-condensing gas) + liquid (refined oil) + solid (char).

First, referring to Figures 1 and 2, the configuration of the thermal decomposition means will be described. The pyrolysis means comprises a pyrolyzer body 210 to maintain a high temperature and low oxygen atmosphere to continuously pyroly decompose combustible materials by indirect heating.

One side of the pyrolyzer body 210 is provided with a main hopper for the input of the pulverized solid combustible material. The combustible combustible material introduced through the main hopper is moved to the pyrolyzer body 210 to pyrolyze.

The main hopper is provided with a sensor so that the amount of combustible combustible material is always stored in the main hopper constantly. The detection sensor automatically adjusts the feeding amount of an input conveyor (not shown) of the solid combustible material so that the solid combustible material does not always fall below the set value.

Inside the pyrolyzer body 210, a pyrolysis screw 220 for transporting and pyrolyzing the combustible material introduced through the automatic input device 400 is rotatably installed by the drive motor 260.

The pyrolysis screw is configured to include a drive shaft 220 connected to the drive motor 230, and a screw blade 221 formed on the outside of the drive shaft 220. The pyrolysis screw is rotated by receiving power from the driving motor 230.

Outside the pyrolyzer body 210 is provided with a pyrolysis chamber 240 made of a heat insulating material to continuously decompose the combustible material by indirect heating by maintaining a high temperature (350 ~ 500 ℃) and low oxygen atmosphere.

On the other hand, among the pyrolysis gases generated during pyrolysis of combustible materials, C ₂ H ₆ , C ₃ H ₈ , C ₅ H ₁₂ (ethane gas, propane gas, butane gas) dominate the main species as light gases with little carbon ring condensation. At the lower side of the pyrolysis chamber 240, a combustion chamber 250 for supplying high temperature heat to the pyrolysis chamber 240, as shown in FIG. 3B, is used as a heat source for pyrolyzing the combustible material transported by burning it. ) And a burner 251 is provided in the combustion chamber 250.

Referring back to FIG. 1, the pyrolyzer body 210 is divided into a first body 211, a second body 213, and a third body 215 in the order of progress of the combustible material. The body is stepped to enlarge the inner diameter step by step to perform the pyrolysis process while going through a three-step process. At this time, the first body 211 and the third body 215 is fixed and installed, the second body 213 is installed to be rotatable.

In the section of the first body 211, the combustible material introduced from the drying means is transferred to the second body 213 by the rotation of the pyrolysis screw 220, and in the section of the second body 213, pyrolysis. Due to the difference in the rotational speed between the screw 220 and the second body 213, the combustible material is moved, and the portion of which thermal decomposition of the preheating, raising the temperature, and vaporizing is substantially performed. In the third body 215 section, the residue which is pyrolyzed is discharged, and the pyrolysis gas is transferred to the second pyrolysis chamber.

Specifically, the configuration of each of the pyrolyzer body 210 will be described.

First, the first body 211 is installed to be fixed, the combustible material introduced from the drying means is moved to the second body 213 while the pyrolysis stream 220 is rotated.

At this time, a first sealing unit 212 is provided between the rear end of the first body 211 and the front end of the second body 213. The first sealing unit 212 has the same configuration as the second sealing 216, which will be described later, is the same as the configuration shown in FIG.

Specifically, the first sealing unit 212 includes a first bushing coupled to the first flange portion formed at the front end of the second body, and a second bushing coupled to the front end of the first bushing. Packings are provided on the inner circumferences of the first bushing and the second bushing, respectively, to double seal between the first body and the second body.

The first sealing unit 212 does not leak the combustible material between the step formed between the first body 211 and the second body 213, the second body 213 in the first body 211 As a result, the influx of flammable substances occurs naturally. Accordingly, pyrolysis of the combustible material moving from the first body 211 to the second body 213 is naturally performed. In addition, due to the first sealing unit 212, the friction generated by the rotation of the first body 211 and the second body 213 is minimized, and the first body 211 and the second body 213 The exact level can be maintained, and prevent the back flow of the combustible material from the second body 213 to the first body 211.

Next, a rotation motor 260 is provided at one side of the second body 213 so that the second body 213 is rotatable. At this time, the second body 213 is supported by the tire 213c so that the second body 213 is stably rotated.

Specifically, power is transmitted to the drive gear 264 through the belts 261 and 262 to transmit the driving force of the rotary motor 260. A driven gear 213b is formed on an outer circumference of the second body 213, and the driving gear 264 and the driven gear 213b are engaged with each other so that the driving force generated in the rotary motor 260 is the second body. The second body 213 is rotated by being transferred to 213.

At least one tire 213c is provided on an outer circumferential surface of the second body 213. The tire 213c is supported by the support roller 266 so that the second body 213 can stably rotate.

At this time, the second body 213 and the drying screw is rotated at a relatively slow speed, the flammability by the difference between the rotational speed of the pyrolysis screw 220 provided in the second body 213 The material is gradually moved compared to the inside of the first body 211. Therefore, it is possible to provide at least three times more heat transfer area than when the second body 213 is fixed, so that more decomposition of the combustible material can be performed in a smaller space.

As the combustible material moves in the section of the second body 213, the combustible material completely vaporizes from solid to liquid, liquid to gaseous material (sometimes, directly sublimates from solid state to gaseous state), Residue of the combustible material which lost its intrinsic properties is moved to the third body 215 section in the form of carbon.

The second sealing unit 216 is provided between the rear end of the second body 213 and the front end of the third body 215. The second sealing unit 216 is coupled to the first bushing 217 coupled to the second flange portion 215 ′ formed at the front end of the third body 215, and to the front end of the first bushing 217. The second bushing 218 is configured to include. Inner circumferences of the first bushing 217 and the second bushing 218 are provided with packings 217a and 218a, respectively, to double seal between the second body 213 and the third body 215. .

The second sealing unit 216 minimizes friction caused by the rotation of the second body 213 and the third body 215, and the second body 213 and the third body 215 are precisely horizontal This can be maintained.

The third body 215 is fixedly installed, the front end portion 215a of the third body 215 and the screw blade 221 of the pyrolysis screw 220 for connection with the second body 213. Correspondingly formed in a circular shape (see Figure 3c), the middle portion 215b of the third body 215 is formed in a streamlined structure so that a space is formed on the upper portion of the screw blade 221 (see Figure 3d). The pyrolysis gas generated at the time of pyrolysis temporarily stays in the space above the screw blades, and the pyrolysis gas can be smoothly moved to the gas retention tower 510 which will be described later.

In addition, the rear end portion 215c of the third body 215 is a section for discharging ash which has undergone all thermal decomposition, and is formed in a circular shape so as to correspond to the outer diameter of the screw blade to minimize the gap between the screw blade and the third body 215. (See FIG. 3E). Accordingly, fly ash generated after pyrolysis is prevented from moving to the gas retention tower 510.

On the other hand, the discharge hole 223 is formed in the screw blade in the section of the second body 213 and the third body 215. Since the discharge hole 223 is formed in the screw blade, the pyrolysis gas generated in the pyrolysis process may naturally move to the gas retention tower 510, and the stirring of the flammable material may be performed smoothly, thereby improving the pyrolysis efficiency.

And one side of the pyrolyzer body 210 is provided with a nitrogen input device (not shown). When a fire occurs due to inadvertent use or malfunction of equipment during operation of the pyrolyzer, it is possible to extinguish the fire by injecting nitrogen into the pyrolyzer body 210 from the nitrogen input device.

When the pyrolysis is completely discharged from the pyrolyzer body 210 is discharged continuously, when the ash is discharged through the valve body 620 such as a slide gate or a rotary valve provided on one side of the third body 215 The air can be blocked from entering the pyrolyzer body 210.

Next, the gas reforming means is a gas detention tower 510 connected to the outlet side of the pyrolyzer body 210 and a first desalination apparatus 550 and a second desalination apparatus for removing chlorine from the reformed gas. And 560.

The spiral screw 520 is provided inside the gas retention tower 510 to sufficiently secure the residence time of the heat source in the process of being discharged after heating the combustible material in the pyrolyzer body 210 by the heat source supplied from the combustion chamber 250. ) Is provided. The gas is discharged while rotating spirally along the spiral screw 520 to secure a time for the gas to stay in the gas retention tower. A driving motor 530 is coupled to an upper end of the spiral screw 520 to provide a driving force for rotating the spiral screw 520 at a predetermined speed.

The pyrolysis gas generated inside the pyrolyzer body 210 is molecularly bonded at a high speed in the inner space of the gas retention tower 510, and detection starts from a substance having a large molecular weight having a long chain of carbon chains.

A wax or tar component mainly composed of 24 or more carbon chains is detected. The tar and dewaxing processes are performed in the inner space of the gas retention tower 510. At this time, the screw blade of the spiral screw 520 rotated by the drive motor 530 is configured to have an outer diameter corresponding to the inner diameter of the gas retention lead is tar or carbonized material attached to the inner peripheral surface of the gas retention tower 510 By scraping the role of separating from the inner circumferential surface of the gas retention tower 510.

The heat source supply chamber 540 is provided on the outside of the gas retention tower 510 to communicate with the pyrolysis chamber 240 through a connection passage. Since the heat source supply chamber 540 is provided, the temperature may be corrected so that the pyrolysis gas rising through the gas retention tower 510 does not condense.

That is, the high heat of about 800 ~ 900 ℃ used as indirect heat in the pyrolysis chamber 240 is introduced into the heat source supply chamber 540 surrounding the gas retention tower 510 while falling to about 500 ~ 600 ℃, the gas The temperature of the retention column 510 is maintained at about 200 ~ 250 ℃. Therefore, the pyrolysis gas in the gas retention tower 510 is transferred to the first desalination unit 550 without condensation.

In the first desalting apparatus 550, the chlorine gas is inevitably generated during the thermal decomposition of the combustible material containing the PVC-based additive having a chlorine component among the combustible materials.

The temperature of the gas retention tower 510 is calibrated to about 200 to 250 ° C. so that no chlorine compound is generated, and the first desalination unit 550 removes the chlorine component by exposing the pyrolysis gas to a basic aqueous solution. do. That is, in the first desalination apparatus 550, by chemical reaction of HCl + NaOH → NaCl + H ₂ O, reaction products having 7 to 23 carbon chains are continuously generated in pyrolysis gas to remove chlorine. .

One side of the first desalination unit 550 of the gas reforming means is provided with a second desalination unit 560 for additionally removing chlorine from the dechlorinated gas.

In the second desalination unit 560, since pyrolysis gas from which chlorine is first removed is continuously formed in the first desalination unit 550, molecular hydrogen is sprayed to quench the pyrolysis gas by spraying an aqueous sodium hydroxide (NaOH) solution. In this way, generation of benzenes can be suppressed, and the formation of long chains in the carbon chain can be suppressed to obtain light oil.

In addition, since the chemical reaction of HCl + NaOH → NaCl + H ₂ O is active, the gas with less carbon chain that is not condensed is discharged in a clean state. Therefore, it is possible to minimize the generation of wax with a long carbon chain.

When pyrolyzing flammable substances containing a large amount of oil components, tar, which is a black viscous liquid, is generated, and its main components are formed by combining with each other in the decomposed gas components while taking a stable form as an aromatic hydrocarbon. In order to minimize the generation of tar, the second desalting apparatus 560 minimizes the space and time at which tar can occur.

One side of the second desalination apparatus 560 is provided with a gas purification means 700 for purifying the dechlorinated pyrolysis gas, and a refining oil producing means 800 for generating refined oil using the pyrolysis gas.

The gas purification means 700 includes a precipitation condensation apparatus for condensing the dechlorinated pyrolysis gas under a stable atmosphere to generate a primary refined oil, and a purification apparatus for improving gas quality. The gas purified through the gas purification means 700 is stored in the gas storage tank through a water seal device and then supplied to the combustion chamber 250 through a pressure regulating device to be used as a gas for combustion.

The refined oil producing means 800 is a storage tank for storing the primary refined oil supplied from the settling condensation device, an oil-separator for oil-separating the primary refined oil stored in the storage tank and the oil-separated refined oil according to the boiling point gasoline, diesel And a distillation column separated by heavy oil.

The carbonization material discharge means is a configuration for discharging the carbonized material generated after pyrolysis from the pyrolyzer body 210, and comprises a discharge hopper 610 formed at the end of the pyrolyzer body 210.

Carbonization material generated after the pyrolysis is continuously discharged through the end of the pyrolyzer body 210, discharge hopper to block the pyrolysis gas discharged from the outside air and pyrolyzer body 210 when the carbonized material is discharged from the outside. The slide gate 620 is provided. The slide gate 620 is preferably configured in at least two stages to maximize the blocking of the outside and prevent malfunction.

The carbonized material continuously discharged through the carbonized material discharge means is discharged to the carbonized material forming means 900 to produce solid fuel. Since the discharged carbonized material is discharged by mixing foreign substances such as superfluous, iron, and non-ferrous metals together, the foreign materials and carbonized material are completely separated through the crushing device and sorting device, and then the foreign materials are removed, and only the carbonized material is passed through the molding device. It produces fuel having a shape, such as briquettes.

Hereinafter, a thermal decomposition method of a solid combustible material according to an embodiment of the present invention will be described.

Solid combustible materials including metal fragments, plastics, paper, industrial combustibles, etc. are shredded to a predetermined size in the crusher after arrival, and the soil, dust, etc. are removed through a sorting machine, and non-ferrous metals are selected and selected. Flammable materials are recycled. The sorted solid combustible material is transferred to a grinder and ground to a relatively small size. The combustible combusted material is secondly re-selected through a magnetic screening device and partly recycled.

The pulverized solid combustible material is introduced into the pyrolysis means through the main hopper, and the combustible material transferred to the pyrolyzer body 210 is pyrolyzed by an indirect heating method of a heat source provided to the pyrolysis chamber 240, and the combustible material is pyrolyzed. When introduced into the body 210, the combustible material that is melted and vaporized while being transferred to the right direction based on FIG. 1 is continuously pyrolyzed by heat applied indirectly in the pyrolysis chamber 240 maintaining an atmosphere of high temperature and low oxygen state. .

At this time, while the second body 213 of the pyrolyzer body 210 rotates together with the pyrolysis screw 220, the second body 213 moves slowly due to the difference in the rotational speed with the pyrolysis screw 220. At least three times more heat transfer area can be provided than when 213 is fixed. Therefore, it is possible to pyrolyze a large amount of combustible material in a small space.

The pyrolysis gas generated after the pyrolysis is stayed in the gas retention tower 510 provided above the pyrolyzer body 210, and is indirectly heated to the combustible material to be pyrolyzed, and then transferred to the dechlorination tower.

The pyrolysis gas transferred after the pyrolysis passes through the first desalting unit 550 and the second desalting unit 560 and then is transferred to the refining oil producing means 800.

And the carbonized material lost the properties after the pyrolysis is discharged through the discharge hopper provided on the lower side of the pyrolyzer body (210). At this time, the discharged carbonized material is discharged by mixing foreign matters such as superfluous, iron, non-ferrous metal, etc., and produces a fuel having a predetermined shape, such as briquettes, through a crusher and a sorting device.

Although the present invention has been described with reference to the embodiment thereof, the present invention is not limited thereto, and various modifications and applications are possible. That is, those skilled in the art will readily understand that many modifications are possible without departing from the gist of the invention.

210: pyrolyzer body
211: first body
213: second body
215: Third body
400: automatic feeding device
510: gas retention tower
610: discharge hopper
700: gas purification means
800: refining oil generating means

Claims (10)

It is provided with a main hopper into which the solid combustible material is injected, and a pyrolysis screw 220 for transporting, melting, and vaporizing the injected combustible material is provided, and the first body 211 and the second body 213 along the conveying direction of the combustible material. And, and the third body 215 is formed to be expanded stepwise, the second body 213 is provided to be rotatable pyrolyzer body 210 for transferring the combustible material by the rotational speed difference with the pyrolysis screw ;
A pyrolysis chamber 240 installed outside the pyrolyzer body 210 to continuously decompose the combustible material by indirect heating by maintaining an atmosphere of high temperature and low oxygen state; And
It is provided on one side of the pyrolysis chamber 240, by burning the non-condensing gas of the pyrolysis gas generated during the pyrolysis of the combustible material to use as a heat source for pyrolyzing the combustible material transferred to the pyrolyzer body 210, the pyrolysis chamber ( Including a combustion chamber 250 for supplying heat to 240,
The inlet portion of the third body 215 is formed in a circular shape so that no gap is formed with the pyrolysis screw.
The middle portion of the third body 215 is formed in a streamline so that a predetermined space can be formed with the pyrolysis screw,
The rear end of the third body 215 is a pyrolysis device of a solid combustible material, characterized in that formed in a circular shape so as not to form a gap with the pyrolysis screw.
The method of claim 1,
And a sealing unit is provided between the first body 211 and the second body 213, and between the second body 213 and the third body 215, respectively.
delete It is provided with a main hopper into which the solid combustible material is injected, and a pyrolysis screw 220 for transporting, melting, and vaporizing the injected combustible material is provided, and the first body 211 and the second body 213 along the conveying direction of the combustible material. And, and the third body 215 is formed to be expanded stepwise, the second body 213 is provided to be rotatable pyrolyzer body 210 for transferring the combustible material by the rotational speed difference with the pyrolysis screw ;
A pyrolysis chamber 240 installed outside the pyrolyzer body 210 to continuously decompose the combustible material by indirect heating by maintaining an atmosphere of high temperature and low oxygen state; And
It is provided on one side of the pyrolysis chamber 240, by burning the non-condensing gas of the pyrolysis gas generated during the pyrolysis of the combustible material to use as a heat source for pyrolyzing the combustible material transferred to the pyrolyzer body 210, the pyrolysis chamber ( Including a combustion chamber 250 for supplying heat to 240,
The pyrolysis apparatus of the solid phase combustible material, characterized in that the discharge hole 223 is formed in the screw blades of the pyrolysis screw provided in the second body 213 and the third body 215 section.
The method according to claim 1 or 4,
The gas pyrolysis apparatus of the solid phase combustible material, characterized in that the gas retention tower (510) for retaining the pyrolysis gas generated during the thermal decomposition of the combustible material for a predetermined time on the upper side of the middle portion of the third body (215) of the pyrolysis body.
The method of claim 5, wherein
Inside the gas retention tower (510), a spiral screw (520) for separating the tar and the carbonized material attached to the inner wall of the gas retention tower is provided with a pyrolysis device of a solid combustible material.
The method of claim 5, wherein
One side of the gas retention tower is a pyrolysis device of a solid combustible material, characterized in that the desalination device for removing chlorine in the pyrolysis gas.
8. The method of claim 7,
Pyrolysis device of a solid combustible material, characterized in that it further comprises a gas purification means (700) for purifying pyrolysis gas from which chlorine is removed from the desalting apparatus.
The method of claim 7, wherein
And refining condensing pyrolysis gas from which the chlorine is removed from the desalting apparatus, and refining condensation producing means (800) for producing gasoline, light oil and heavy oil according to boiling points in the distillation column.
The method according to claim 1 or 4,
A pyrolysis device for solid phase combustible material, characterized in that it further comprises a carbon material discharge means for continuously discharging the carbon material generated after pyrolysis from the pyrolysis chamber (240).

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