KR20230030990A - Organic waste disposal device for increasing calories of the by-product - Google Patents

Abstract

The present invention relates to an organic waste disposal device for treating organic waste remaining after purification of food waste, livestock waste, or waste water containing organic matters, the organic waste disposal device for increasing the calorific values of by-products, wherein waste is treated by drying and carbonization, and at the same time, the gas generated in the drying process is heated and used in the carbonization process, the tar generated in the carbonization process is reused as an auxiliary fuel so as to increase the calorific values of carbonized materials, the drying efficiency of a dryer is increased by accelerating the discharge of drying gas, and the internal temperature of a carbonizer with high safety can be effectively controlled to increase the utility of the carbonized materials. To achieve this, the organic waste disposal device comprises the dryer (100), the carbonizer (200), a hot air supply unit (300), and a pyrolysis unit (400).

Description

Organic waste disposal device for increasing calories of the by-product}

The present invention relates to an organic waste treatment apparatus for treating organic waste remaining after purifying food waste, livestock waste, or wastewater containing organic matter, and treating the waste by using a method of drying and carbonization, and at the same time drying process The temperature of the gas generated in the carbonization process is raised and used in the carbonization process, and the gas generated in the carbonization process is recycled as an auxiliary fuel to reduce energy costs and improve the calorific value of carbonized materials by using the tar generated in the carbonization process. The present invention relates to a dryer with improved drying efficiency by facilitating discharge and an organic waste treatment device for improving the calorific value of by-products that can effectively control the internal temperature of a highly safe carbonizer to improve the utilization of carbonized materials.

In general, organic waste is a general term for domestic waste generated from homes or restaurants, or sludge generated from sewage/wastewater treatment plants. The amount of sludge generated increases every year due to the advanced sewage treatment since 2017 and the strengthened environmental laws in 2018. Since these organic wastes contain a large amount of moisture, are easily corroded and generate odors, research on treatment methods including landfill or incineration is being actively conducted.

For example, a method of landfilling in a landfill has been proposed as a method of treating the organic waste, but the landfilling method is practically prohibited in accordance with related laws as well as environmental aspects, and the approved landfill is saturated, so it is no longer effective. There was a problem of losing the .

Accordingly, a method of incineration and carbonization of the organic waste has emerged, and a method of incinerating the organic waste at a high temperature to utilize the heat of incineration or discharging it as a carbonized material having an extremely low moisture content through a drying and carbonization process to obtain the above Carbonized materials are being used for auxiliary fuel, coagulant, and filling soil in thermal power plants.

However, it is known that treatment methods such as incineration and carbonization of organic waste generate a large amount of harmful gas, and landfill generates leachate, which is a problem of second environmental pollution. Multi-screw type dryers for drying and using as auxiliary fuel have poor drying efficiency due to difficulty in smoothly discharging dry gas. Use is limited. A carbonization method is developed and operated for the organic waste, which is environmentally friendly and has excellent civil complaint reduction, but gas transportation is not smooth due to the tar generated during the carbonization process. It has the disadvantage of generating, and a lot of civil complaints are generated due to the occurrence of odor.

Therefore, it is possible to suppress civil complaints by removing dust and harmful gases generated in the drying/carbonization process by itself, and at the same time, it is possible to reduce maintenance costs by recycling carbonized gas as thermal energy, and to reduce facility costs by simplifying facilities. There is a need for the development of an organic waste treatment device.

1. Registered Utility Model Publication No. 20-0251419 'Organic Waste Disposal Device' (Application Date 2001.07.16) 2. Patent Publication No. 10-1997-0026956 'Organic waste treatment device' (application date 1995.11.21) 3. Korean Patent Registration No. 10-1995128 'Microwave reformer for gas reforming' (application date 2017.10.18) 4. Korean Patent Registration No. 10-0867337 'Burner for Combustion of Powdered Fuel Manufactured from Food Waste' (Application Date 2007.06.25)

The present invention has been made to solve the above problems, and it is possible to pyrolyze moisture and odor contained in the gas generated in the drying process, and supply the pyrolyzed and high temperature gas to a carbonizer for recycling, and in the carbonization process An object of the present invention is to provide an organic waste treatment device that maximizes utilization by reusing generated gas as an energy source to create economic effects and at the same time increase the calorific value of carbide obtained as a by-product.

An organic waste treatment apparatus for improving the calorific value of by-products of the present invention includes a dryer (100) for receiving organic waste to one side and drying moisture contained in the organic waste; a carbonizer 200 that receives the dried organic waste from the dryer 100 and carbonizes the organic waste; A hot air supply unit 300 equipped with a burner 310 on one side to supply hot air to the dryer 100 to heat it; including, but receiving the dry gas generated in the dryer 100, the hot air supply unit 300 A thermal decomposition unit 400 for purifying by thermal decomposition inside and supplying the purified gas whose temperature has risen due to thermal decomposition to the carbonizer 200; is characterized in that it is further provided.

In the present invention, a path through which the dried organic waste moves to the carbonizer 200 is a gas that is opened only when the dried organic waste moves to prevent the dry gas from entering the carbonizer 200. A blocking unit 500; may be further provided.

In addition, while receiving the carbonized gas generated in the carbonizer 200 and raising the temperature, the less decomposed material is decomposed to obtain a gas in a form that is easy to burn and used as an auxiliary fuel, and the gas temperature is raised so that the liquid tar is extracted separately. A unit 600 is further provided, and the carbonized gas passing through the gas heating unit 600 is moved to the hot air supply unit 300.

On the other hand, the present invention is provided between the dryer 100 and the carbonizer 200, and a mixture obtained by receiving and mixing the liquid tar extracted from the carbonized gas and the dried organic waste discharged from the dryer 100 A mixer 1000 passing to the carbonizer 200; may be further provided. The sludge mixed with liquid tar is partially decomposed and gasified during the carbonization process, and some is adsorbed to the carbide to improve the calorific value of the carbide.

The carbonization machine 200 of the present invention includes a carbonization case 210; A stirring blade 220 for moving the dried organic waste from one side of the carbonization case 210 to the other side; A case cover 230 for sealing the open upper side of the carbonization case 210; A hot air case 240 surrounding the outside of the carbonization case 210 and receiving hot air from the pyrolysis unit 400; including, but carbonized gas moves between the case cover 230 and the stirring blade 220 It is characterized in that the fluid movement space (S2) is further formed.

The dryer 100 of the present invention includes a first drying tube 110; A first screw 120 of a double cylinder type installed rotatably inside the first drying tube 110 and moving organic waste from one side to the other side; A second drying tube 130 that surrounds the outside of the first drying tube 110 and receives the organic waste primarily dried in the first drying tube 110; a hot air case 140 that surrounds the outside of the second drying tube 130 and receives heat energy from the heat supply unit 300; Including, but the rotation center axis (A) of the first drying pipe 110 and the first screw 120 is disposed in a state eccentric at a predetermined interval from the central axis (A1) of the first drying pipe 130 to be characterized

The inner diameter of the second drying pipe 130 of the present invention maintains a state adjacent to the outer edge of the first drying pipe 110, but one side of the second drying pipe 130 is the center of rotation axis (A) It is characterized in that a gas flow passage 131 protrudes by the spaced apart distance from the central axis A1 and guides the movement path of the carbonized gas generated during drying.

The present invention reuses each gas generated during drying and carbonization of organic waste as heat energy and auxiliary fuel to reduce energy consumption costs in the treatment of organic waste, and does not require a separate facility to remove odors, thereby reducing production costs. can reduce

In addition, by installing a gas heating unit to improve the quality of carbonized gas, the amount of carbonized gas used as auxiliary fuel is increased to reduce energy costs, and since undecomposed liquid tar is mixed with dry sludge, the calorific value of carbonized material can be improved. .

In addition, a plurality of grooves are formed at the end of the screw that moves the sludge, and a non-continuous screw is used to prevent sludge agglomeration generated during the drying process of organic waste and to facilitate the flow of gas generated during the drying and carbonization process. It has the advantage of increasing drying and carbonization efficiency.

1 is a schematic diagram for helping the overall understanding of the present invention.
Figure 2 is a schematic view showing one embodiment of the dryer of the present invention.
Figure 3 is a perspective view showing one embodiment of the main configuration and shape of the screw of the present invention.
Figure 4 is a cross-sectional view showing the main configuration of the carbonizer of the present invention.
Figure 5 is a partial schematic diagram showing an embodiment of the dust collector of the present invention.

Hereinafter, an embodiment of an organic waste treatment apparatus for improving the calorific value of by-products according to the present invention will be described in detail with reference to the drawings.

Referring to FIG. 1 , the present invention includes a dryer 100, a carbonizer 200, a hot air supply unit 300, and a thermal decomposition unit 400.

The dryer 100 extends to a certain length in the horizontal direction and receives a certain amount of organic waste through an inlet provided on one side. The dryer 100 has a hollow interior so that the input organic waste can move along the extension direction of the dryer 100. At this time, a separate screw 101 for moving the organic waste from one side of the dryer 100 to the other side may be further provided inside the dryer 100 .

The dryer 100 has the purpose of stirring the organic waste and drying the moisture contained in the organic waste at the same time. On one side of the dryer 100, a sludge feeder 102 for introducing organic waste into the dryer 100 may be further provided. The sludge feeder 101 is manufactured in the form of a rotary valve and an airlock valve to block the inflow of air by disconnecting the inner space and the outer space of the dryer 100, and can uniformly supply a certain amount of organic waste. The delivered organic waste is dried while moving from one side to the other side along the inside of the hollow dryer 100.

The carbonizer 200 extends in the longitudinal direction and has a hollow shape inside to receive the dried organic waste from the dryer 100 . The carbonizer 200 pyrolyzes and carbonizes organic waste with high-temperature thermal energy, and generates pyrolyzed organic waste (hereinafter referred to as carbide). The generated carbide may be transferred to and stored in a separate carbide storage 700 provided on one side of the carbonizer 200.

The hot air supply unit 300 includes a burner 310 that generates hot air, and the hot air generated by the burner 310 transfers thermal energy to the dryer 100 to heat the dryer 100 .

Inside the hot air supply unit 300, in order to prevent the flame of the burner 310 from directly contacting the inner wall surface of the hot air supply unit 300, a flame induction pipe 320 surrounding the flame of the burner 310 is emitted. This may be further provided.

Referring to FIG. 1 , a thermal decomposition unit 400 is further provided inside the hot air supplier 300, and is heated by receiving high-temperature thermal energy from the hot air supplier 300.

Meanwhile, when hot air is supplied to the dryer 100 to dry the organic waste, drying gas is generated inside the dryer 100 . At this time, the generated dry gas is transported to the pyrolysis unit 400, and is pyrolyzed while passing through the heated pyrolysis unit 400 to be purified into a purified gas.

More specifically, the dry gas generated as moisture contained in organic waste is evaporated, dried, and thermally decomposed includes a significant amount of undecomposed organic matter, methane gas, hydrogen, carbon monoxide, and odorous substances. When such a dry gas is released into the atmosphere, it becomes a main culprit of air pollution and causes damage to the surrounding environment. To solve this problem, the dry gas is pyrolyzed while passing through the pyrolysis unit 400 to purify contaminants, humidity, and odor contained in the dry gas.

On the other hand, the purified gas purified by passing through the thermal decomposition unit 400 has a high temperature as odorous substances are thermally decomposed. This cleaning gas is delivered to the carbonizer 200 to heat the carbonizer 200. At this time, the purified gas passing through the pyrolysis unit 400 is partially transferred to the carbonizer 200 through a bypass pipe (not shown) and used as a heat source for carbonization. The amount of heat transferred to the carbonizer is the degree of carbonization (complete carbonization or The supply amount is adjusted according to torrefaction), and the rest is released into the atmosphere.

The temperature of the purification gas may be adjusted according to the time during which the purification gas is stagnant in the pyrolysis unit 400 . That is, while the high-temperature purification gas heats the carbonizer 200, the organic waste accommodated in the carbonizer 200 may be carbonized or torrefied.

Referring to FIG. 1 , a gas blocking unit 500 is further provided in a path along which organic waste dried from the dryer 100 to the carbonizer 200 moves. The gas blocking unit 500 moves from the dryer 100 to the carbonizer 200 to prevent the dry gas inside the dryer 100 from flowing into the carbonizer 200 when the organic waste moves to the carbonizer 200. It is opened only when the dried organic waste is moved, and the movement path is blocked when the movement is completed.

Referring to FIG. 1 , a gas heating unit 600 may be further provided between the carbonizer 200 and the hot air supply unit 300 . The gas heating unit 600 receives the carbonized gas and has the purpose of raising the temperature of the carbonized gas to extract liquid tar from the carbonized gas.

In addition, the gas heating unit 600 thermally decomposes a significant portion of the undecomposed organic matter included in the introduced carbonized gas, and then transfers it to the hot air supply unit 300 so that it can be used as auxiliary fuel.

The gas heating unit 600 includes a first gas inlet pipe 610 and a second gas inlet pipe 620 .

The first gas inlet pipe 610 has a hollow inside in a tubular shape having a predetermined diameter, and receives carbonized gas to one side. At this time, the first gas inlet pipe 510 extends in the longitudinal direction so that the carbonized gas can stay.

The second gas inlet pipe 620 has a larger diameter so as to surround the outside of the first gas inlet pipe 610, and receives hot air from the hot air supplier 300 to one side to heat the first gas inlet pipe 610. do. The hot air passes through the second gas inlet pipe 620 and then moves to the dryer 100 .

Inside the first and second gas pipe 610 and 620, first and second wings 611 and 621 formed in a spiral shape may be further provided, respectively.

The heating temperature of the gas heating unit 600 is maintained at about 800°C or higher, preferably between 800 and 1200°C. When the carbonized gas generated in the carbonization process passes through the gas heating unit 600, moisture and foreign substances included in the carbonized gas are thermally decomposed, and tar included in the carbonized gas can be extracted as a liquid phase. And, the remaining carbonized gas is transferred to the heat supply unit 300 and can be used as auxiliary fuel.

Meanwhile, a mixer 1000 may be further provided between the dryer 100 and the carbonizer 200 to receive and mix the liquid tar extracted from the carbonized gas and the dried organic waste discharged from the dryer 100. The mixture mixed in the mixer 1000 is supplied to the carbonizer 200 and the carbonization process proceeds. In this way, since tar is injected and carbonized, a certain amount of undecomposed tar is adsorbed on the carbide, so the calorific value of the carbide increases and can be used as an auxiliary fuel such as coal. The decomposed tar is gasified and can be used as an auxiliary fuel. Therefore, it is possible to obtain the effect of reducing the sludge treatment fuel cost.

On the other hand, the dry gas may also pass through the gas heating unit 600, which can improve purification efficiency by first removing foreign substances contained in the dry gas, and after raising the temperature of the dry gas to a certain extent, the thermal decomposition unit ( 400), it is possible to prevent a phenomenon in which the temperature of the thermal decomposition unit 400 is rapidly lowered.

Referring to FIG. 2 , the dryer 100 includes a first drying tube 110 , a first screw 120 , a second drying tube 130 and a hot air case 140 .

The first drying tube 110 has a cylindrical tube shape with a hollow inside to receive organic waste to one side.

The first screw 120 is installed to rotate inside the first drying tube 110 and primarily dries the dried organic waste while stirring. At this time, the inside (rotation shaft) of the first screw 120 is hollow along the longitudinal direction of the first screw 120, and hot air can be received through the hollow interior. (not shown)

As the first screw 120 is heated by the received hot air, the internal temperature of the first drying tube 110 is increased, and the inside and outside of the first drying tube 110 may be heated simultaneously. Thus, drying efficiency of the dryer 100 can be improved.

The second drying pipe 130 is formed in a cylindrical shape surrounding the outside of the first drying pipe 110, and receives organic waste primarily dried from the first drying pipe 110. The first drying tube 110 is installed to rotate inside the second drying tube 130, and a plurality of stirring blades are formed on the outer surface of the first drying tube 110. As the first drying tube 110 rotates, organic waste is moved and stirred inside the second drying tube 130, and drying efficiency can be improved by performing secondary drying.

The hot air case 140 surrounds the outside of the second drying tube 130 to heat the outside of the second drying tube 130 . Then, the inside of the second drying tube 130 is heated by receiving the hot air from the pyrolysis unit 400 .

Referring to FIG. 2, the rotational center axis (A) of the first screw 120 and the first drying pipe 110 is arranged eccentrically at a predetermined interval from the central axis (A1) of the second drying pipe 130. 2 rotates inside the drying tube 130. That is, the diameter of the second drying pipe 130 is larger than the diameter of the first drying pipe 110, and in this way, the rotation center axis of the first screw 120 and the first drying pipe 110 ( When A) is eccentric, a predetermined gap is generated between the outer surface of the first drying pipe 110 and the inner surface of the second drying pipe 130.

At this time, since the drying gas generated during drying of the organic waste moves along the formed gap, the drying gas can be smoothly discharged from the inside of the dryer 100 .

On the other hand, the inner diameter of the second drying pipe 130 maintains a state adjacent to the diameter of the stirring blade formed outside the first drying pipe 110, and one side of the second drying pipe 130 is connected to the rotation center axis A It protrudes as much as the spaced distance of the central axis A1 to facilitate gas movement between the first drying pipe 110 and the second drying pipe 130. The dry gas generated during the drying process can move along the formed gas flow passage 131, so that the dry gas can be smoothly discharged.

In addition, the edge of the gas flow path 131 may be formed in an arc shape having a certain radius of curvature. At this time, the angle θ formed by the radius of curvature of the gas flow path 131 is the rotation center axis A or When centered on the axis A1, an angle of 5 to 15° may be formed.

As an embodiment of the second drying pipe 130, a pair of extension plates 132 facing each other and an end of the extension plate 132 are formed on one side of the second drying pipe 130 to have a predetermined radius of curvature. It includes a finishing plate 133 having a. The extension plate 132 is formed such that its ends are inclined to face each other in order to minimize the space between the stirring blades and the second drying pipe 130 .

The finishing plate 133 is also formed to have a predetermined radius of curvature to provide space for the gas passage 131, and dry gas can be smoothly collected and transported through the provided gas passage 131.

Due to this, when the first drying tube 110 rotates inside the second drying tube 130, a state in which the agitation wings formed on the first drying tube 110 and the inner surface of the second drying tube 130 are in close contact. can keep As a result, it is possible to prevent a phenomenon in which smooth rotation of the first drying pipe 210 is not progressed due to stenosis of the dried organic waste between the agitating blade and the inner surface of the second drying pipe 130 .

Referring to FIG. 4 , the carbonizer 200 includes a carbonization case 210 , a stirring blade 220 , a case cover 230 and a hot air case 240 .

The upper side of the carbonization case 210 is open, and a receiving space S1 is formed therein to receive organic waste. Preferably, the lower side of the carbonized case 210 may have a hemispherical shape.

The stirring blade 220 is rotatably mounted inside the carbonization case 210 and moves the delivered dried organic waste while stirring the carbonization case 110 from one side to the other.

At this time, referring to FIG. 3, the stirring blade 220 extends to a predetermined length, and is mounted inside the carbonization case 210 to move the rotating shaft 221 and the organic waste when the shaft 221 rotates. It includes screw blades 222 forming a spiral shape wound around the outer surface of the shaft 221 so as to do so. At this time, the screw blades 222 are characterized in that a plurality of stirring grooves 222-1 are formed along the edge of the screw blades 222 at regular intervals.

Referring to FIG. 2 , the case cover 230 seals the upper side of the open carbonization case 210 . At this time, the carbonization case 210 is formed in a U-shape, and the case cover 230 is provided on the open upper side to form a predetermined space between the carbonization case 110 and the stirring blade 220.

In more detail, the open top of the carbonization case 210 is further extended to further form a fluid movement space S2 between the edge of the stirring blade 220 and the case cover 230. The carbonized gas generated in the carbonizer 100 may move along the formed fluid movement space S2.

The hot air case 240 is formed to surround the outside of the carbonization case 210 to heat the outside of the carbonization case 210 . In addition, the organic waste may be carbonized or torrefied by heating the carbonization case 210 by receiving hot air from the thermal decomposition unit 400 .

As another embodiment of the dryer 100, the dryer 100 may have the same shape and structure as the carbonizer 200, and detailed descriptions are the same as those of the carbonizer 200, and thus will be omitted.

In carbonization, when organic waste such as sludge is heated to a high temperature in an anoxic state, thermal decomposition begins with the generation of water and gas. Carbonized matter corresponds to a residue mainly composed of carbon from the evaporation of residual moisture and gas from dried organic waste. Therefore, when heating the inside of the carbonizer 200, it is preferable to heat after blocking it from the outside so that air does not flow into the carbonizer 200.

On the other hand, the carbide thermally decomposed in the carbonizer 200 corresponds to a high-temperature product, and there is a risk of spontaneous ignition due to the temperature of the carbide itself. In order to prevent this, water is sprayed and stored on a path on which the carbide moves to the carbide storage 700 so that the humidity of the carbide stored in the carbide storage 700 can be maintained at about 8%.

Referring to FIG. 1 , the carbonized gas discharged from the carbonizer 200 moves to the hot air supply unit 300 or the burner 310 and can be used as auxiliary fuel.

Referring to FIG. 1 , the hot air that heats the dryer 100 and the carbonizer 200 and is discharged to the atmosphere passes through a separate dust collecting unit 800 and is discharged into the atmosphere. The dust collecting unit 800 may preferably have a cyclone structure. The exhaust gas passing through the dust collecting unit 800 can be released into the atmosphere or used to heat combustion air supplied to the hot air supply unit 300 to increase combustion efficiency.

A bag filter unit 802 for filtering fine dust included in the hot air passing through the dust collecting unit 800 may be provided on one side of the dust collecting unit 800, and the bag filter unit 802 includes a HEPA filter with a filter net, It may correspond to a dust filter or the like.

At this time, a cooling unit 801 may be provided between the dust collecting unit 800 and the bag filter unit 802 to cool the hot air. The cooling unit 801 may prevent the bag filter unit 802 from being melted, deformed, or damaged due to high temperature.

The exhaust gas, which has been purified and filtered through the bag filter unit 802 and the dust collection unit 800, is released into the air, and a suction fan (not shown) is provided in front of the bag filter unit 802 for the purpose of circulating hot air. This may be additionally provided.

Meanwhile, the cooling unit 801 of the dust collecting unit 800 may introduce external air, and heat exchange between the high-temperature hot air passing through the cooling unit 801 and the external air may cool the hot air. At this time, the introduced external air is heated while performing heat exchange, and the heated external air may be supplied as combustion air of the hot air supply unit 300 . Therefore, the advantage of improving the combustion efficiency of the hot air supply unit 300 is provided.

1, a separate blower (not shown) is provided between the dryer 100 and the gas heating unit 500 and between the pyrolysis unit 400 and the carbonizer 200 to move hot air and gas. .

In addition, the dryer 100 and the carbonization machine 200 may further include a hot air control unit 900 that detects the internal temperature of each and controls the operation of the installed blower. The internal temperature of the dryer 100 and the carbonizer 200 may be adjusted by adjusting the air volume of the blower based on the temperature data measured by the hot air control unit 900 .

The present invention having such a configuration can control (adjust) the drying temperature and the carbonization temperature, expand the range of utilization of the carbide by controlling the degree of carbonization of the carbide, and easily use the generated dry gas and carbonized gas. This has the advantage of reducing energy consumption costs associated with organic waste treatment.

100: dryer 200: carbonizer
300: hot air supply unit 400: thermal decomposition unit

Claims (7)

a dryer (100) for receiving organic waste to one side and drying moisture contained in the organic waste;
a carbonizer 200 that receives the dried organic waste from the dryer 100 and carbonizes the organic waste;
A hot air supply unit 300 provided with a burner 310 on one side to supply hot air to the dryer 100 to heat it; including,
A thermal decomposition unit 400 that receives the dry gas generated from the dryer 100, pyrolyzes and purifies it inside the hot air supply unit 300, and supplies the purified gas whose temperature has risen due to pyrolysis to the carbonizer 200 ; Organic waste treatment apparatus for improving the calorific value of by-products, characterized in that further provided. According to claim 1,
In the path where the dried organic waste moves to the carbonizer 200, a gas blocking unit 500 that is opened only when the dried organic waste moves to prevent the dry gas from entering the carbonizer 200 ; Organic waste treatment apparatus for improving the calorific value of by-products, characterized in that further provided. According to claim 1,
A gas heating unit 600 for receiving the carbonized gas generated in the carbonizer 200 and raising the temperature of the carbonized gas to extract liquid tar from the carbonized gas is further provided,
Organic waste treatment device for improving the calorific value of by-products, characterized in that the carbonized gas passing through the gas heating unit 600 moves to the hot air supply unit 300. According to claim 3,
It is provided between the dryer 100 and the carbonizer 200, and a mixture obtained by receiving and mixing the liquid tar extracted from the carbonized gas and the dried organic waste discharged from the dryer 100 is mixed with the carbonizer 200 Organic waste treatment apparatus for improving the calorific value of by-products, characterized in that it comprises a; According to claim 1,
The carbonizer 200 includes a carbonization case 210;
A stirring blade 220 for moving the dried organic waste from one side of the carbonization case 210 to the other side;
A case cover 230 for sealing the open upper side of the carbonization case 210;
A hot air case 240 that surrounds the outside of the carbonization case 210 and receives hot air from the pyrolysis unit 400;
Organic waste treatment device for improving the calorific value of by-products, characterized in that a fluid movement space (S2) in which carbonized gas moves is further formed between the case cover 230 and the stirring blade 220. According to claim 1,
The dryer 100 includes a first drying pipe 110;
A first screw 120 rotatably installed inside the first drying tube 110 and moving organic waste from one side to the other side;
A second drying tube 130 that surrounds the outside of the first drying tube 110 and receives the organic waste primarily dried in the first drying tube 110;
a hot air case 140 that surrounds the outside of the second drying tube 130 and receives heat energy from the heat supply unit 300; Including,
The by-product, characterized in that the central axis of rotation (A) of the first drying pipe (110) and the first screw (120) is disposed eccentrically at a predetermined interval from the central axis (A1) of the first drying pipe (130) Organic waste treatment device for improving the calorific value of According to claim 6,
The inner diameter of the second drying pipe 130 maintains a state adjacent to the outer edge of the first drying pipe 110,
One side of the second drying pipe 130 protrudes as much as the distance between the central axis of rotation A and the central axis A1 and has a gas flow path 131 guiding the movement path of the drying gas generated during drying. Organic waste treatment apparatus for improving the calorific value of by-products, characterized in that further provided.

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