KR200226953Y1 - A carbonizing treating appartus for waste matter - Google Patents

Abstract

It is an object of the present invention to provide a carbonization and exhaust system that efficiently dehydrates and carbonizes household wastes and at the same time makes production costs low and completely removes odors and dioxins. The present invention paints a heat-resistant far-infrared radiation ceramic layer on the inner wall of the carbonization tank, and installs a heater for electricity, gas, or oil on the outer side of the far-infrared radiation ceramic layer made by natural drying. In addition, the carbonization tank is detachably installed in the carbonization tank for household waste, and a plurality of catalyst devices, in order to remove organic components such as odors and soot in the exhaust gas discharged from the carbonization tank, An anion treatment water tank was installed. In addition, it is to install a far-infrared radiation honeycomb heater for use in carbonization, such as salt sheet.

Description

A CARBONIZING TREATING APPARTUS FOR WASTE MATTER}

The present invention relates to waste carbonization and exhaust equipment suitable for use in boarding vehicles such as ships, or in general houses, commercial or industrial facilities, and in particular, by irradiating far-infrared radiation to the treated carbide efficiently, drying, pyrolysis and carbonization The present invention relates to a carbonization and exhaust apparatus for treating waste represented by household waste or plastic products, which is designed to be efficiently used and used together to remove various components of exhaust gas so that various environmental problems do not occur.

In addition to incineration, carbonization is well known as a treatment technique for waste plastic film (sheet) used in household waste or a vinyl house. This carbonization treatment technique is a method of carbonizing waste by heat treatment in the absence of oxygen, but there is a problem in that it is not satisfactory in terms of treatment efficiency and cannot be easily installed and used in ships including fishing boats.

Accordingly, an object of the present invention is to solve the above-mentioned shortcomings, and to efficiently carbonize the waste vinyl film generated from household waste or vinyl house, and at the same time, the production cost is low, and moisture, odor, dioxin, etc. To provide a carbonization and exhaust system for wastes that can be completely removed.

In order to achieve the above object, in the carbonization treatment apparatus of claim 1, in the carbonization treatment apparatus of waste, a heat-resistant far-infrared radiation ceramic layer is formed on the inner wall surface of the carbonization tank in which the waste is accommodated, and at the same time a far-infrared radiation ceramic layer A carbonization treatment unit provided with a first heating heater on an outer side of the carbonization unit; A pressurizing means installed to move up and down from the upper portion of the carbonization treatment portion and pressurizing the waste contained in the carbonization tank during the downward movement, and contacting through the carbonization tank and the net at the bottom of the carbonization treatment portion facing the pressurizing means. Carbide moisture treatment unit that is installed so as to store the moisture discharged from the carbonization waste and the second heating heater disposed on the lower portion of the water reservoir directly to apply heat; A stirring device which is driven by a motor installed in the carbonization tank to agitate the carbonated material dehydrated in the carbide water treatment unit and freely detachable from the motor in the carbonization tank; The inside and outside of the carbonization tank is installed to be in contact with the upper part of the carbonization tank in which the stirring device is installed to remove dust, odor and smoke components in the exhaust gas discharged from the carbonization tank, and to remove odor and smoke. An exhaust treatment unit for i); And a water tank at the final stage of the exhaust treatment unit that finally introduces and treats exhaust gas in water to remove environmental pollutants such as soot.

In the carbonization apparatus of claim 2, in the carbonization apparatus of claim 1, a honeycomb-type far-infrared radiator heater is further provided on the head of the carbonization tank, and is separately attached to the workpiece in the carbonization tank. By or in combination with a far-infrared radiation ceramic layer is characterized in that the carbonization treatment.

In the carbonization apparatus of claim 3, the carbonization apparatus of claim 1 is characterized in that the heat-resistant far-infrared radiation ceramic layer is formed by coating a far-infrared radiation ceramic coating on the inner surface of the carbonization tank.

In addition, in the carbonization apparatus of claim 4, in the carbonization apparatus of claim 1, the pressurizing means pressurizes the carbides introduced into the carbonization tank, and a pressure plate on which a carbide input part is formed is loosely coupled to the pressure plate. And two screw rods movably inserted in the case cover, and stepping motors engaged with each other of the screw rods on the upper surface of the carbonization tank through electric gears.

The carbonization apparatus of claim 5, further comprising: a carbonization apparatus of claim 1, wherein the exhaust treatment unit comprises: a discharge pipe configured to communicate with the outside from the carbonization tank; And first to third catalysts installed in order to sequentially contact the discharge pipe in order to remove odors, dust, carbon monoxide, dioxins, and the like from the fumes discharged from the carbonization tank.

The carbonization apparatus of claim 6 is the carbonization apparatus according to claim 1, wherein the air bubbler is operated by a vacuum pump that sucks exhaust gas into the water tank, and introduces the air bubbler into the water tank. It is characterized in that it is further provided with ionic stones to anionize the flowing water, such as gas discharged from.

Further, the carbonization apparatus according to claim 7 is a condenser for removing water generated from the carbides in the carbonization tank in the vicinity of the exhaust treatment unit in the exhaust treatment unit, and the condenser via A third heating heater is further provided for heating catalysts for treating one exhaust gas.

The carbonization apparatus according to claim 8, according to claim 1 or 5, is arranged in mutual communication between the catalyst and the water tank in the exhaust pipe of the exhaust treatment unit to smoothly discharge the exhaust gas via the exhaust pipe. To further characterized in that it further comprises a cooling fan, blower and exhaust cylinder.

The present invention having the above-described configuration, by heating the heat-resistant far-infrared radiation ceramic layer with a heating means including an electric heater, radiates a large amount of far-infrared radiation at its heating temperature, and the emitted far-infrared radiation is a household waste ( Organic wastes irradiated with organic matters and absorbing specific far infrared rays generate heat during molecular movements, and are dried by evaporation of water from household wastes.

In addition, the carbonization time may be greatly changed in the case of excessive moisture in household waste and industrial waste, so that the carbonization treatment of carbides can be processed quickly and efficiently by compressing by pressurizing means operated by stepping motor before operation. Can be.

In addition, the carbonization tank is almost in a closed state, and household waste is heated at 250 to 350 ° C. by heating means, and since it is oxygen-free, the household waste is not oxidized, causes drying, thermal decomposition, low molecular weight, Groups such as hydrogen and chlorine around the -CC-bond are separated and the household waste is then carbonized.

By well agitating the household waste with the stirring device installed in the carbonization tank, the household waste is mixed evenly, and the far-infrared irradiation is efficiently carried out while contacting and approaching the far-infrared radiation layer by moving with stirring.

Since the mixing of so-called salt ratio films and sheets is difficult to stir, a detachable stirring device is installed, and a honeycomb type far infrared radiation heater is installed on the head of the carbonization tank, and the honeycomb type far infrared radiation heater and carbonization of the head are treated. It carbonizes while being thermally decomposed efficiently by a heating device such as an infrared heater and an infrared heater radiating by heating the far-infrared ceramic layer of the inner wall of the bath. However, honeycomb-type far infrared radiation heater of tofu can be used for disposal of household waste. In addition, this heater can be carbonized by a single drive according to the to-be-processed object.

On the inner surface of the carbonization tank equipped with a detachable stirring device for stirring household wastes, a far-infrared radiation ceramic is applied by applying heat-resistant paint (maximum temperature characteristic 1000 ℃) of far-infrared radiation ceramic type that arrives by natural drying in the center. Form a layer. The outer side of this carbonization tank is provided with a heating device made of a heater block in which a nichrome wire, a heating wire (heater) such as this canal wire is embedded in a groove coated with ceramic insulation, and the heat generated by heating the carbonization tank is heated. Based on the far-infrared radiation emitted from the far-infrared radiation ceramic paint on the inner wall of the carbonization tank, it is possible to quickly dry and thermally decompose the household wastes in the carbonized tank closed by the far-infrared radiation heat and carbonize the household waste. The electric heater method is most easily used as a heating means, but a heating means using gas, oil, or the like as a heat source may be used depending on conditions.

In the case of carbonization, by stirring a large amount of household waste with a stirring device, the living garbage inside the carbonization tank is also brought into contact with or close to the inner wall of the carbonization tank, and the far infrared rays radiated from the far-infrared radiation ceramic coated on the inner wall of the carbonization tank Effectively reach the whole household waste, the above-mentioned far-infrared ray effect is appeared, and it is possible to efficiently dry, pyrolyze and carbonize the household waste.

When carbonizing vinyl sheets and various plastic wastes used in agricultural vinyl houses in a carbonization device, remove the detachable agitator installed in the carbonization tank, install a honeycomb type far-infrared radiation ceramic heater in the front of the carbonization tank, and Plastic waste, such as vinyl sheets, may be introduced into a carbonization tank, heated in a sealed state, and thermally decomposed and carbonized by far-infrared radiation. At this time, heating devices provided around the carbonization layer may be operated simultaneously. In addition, for waste that is hard to be carbonized, a honeycomb-type far-infrared radiation ceramic heater can be used as a means for enhancing far-infrared radiation as it is provided with a stirring device. That is, the honeycomb far-infrared radiation ceramic heater is formed by passing a honeycomb structure supporting member to form a far-infrared radiation type and a heater containing a far-infrared radiation ceramic, and this causes a far-infrared radiation to be treated. There are two ways.

Evaporative components such as odorous components and low-molecular organic substances generated from household wastes, vinyl sheet waste, etc. are catalysts installed in the first stage. Hazardous gases such as carbon monoxide are completely oxidized, smoke removed, and odor removed under the temperature condition of 350 ℃. In the second stage, a known catalyst is used to completely oxidize non-decomposable organic substances such as dioxins to inorganic substances under a temperature condition of 220 ° C.

The exhaust gas, mineralized with the catalytic device, is cooled, for example, then flowed into the water tank and ionized, where it is then bubbled by an air bubbler, and impurities are dissolved and removed in water and then released into the atmosphere. .

The detachable stirring device for stirring the household wastes installed in the carbonization tank is connected to the stirring motor in the lower portion of the carbonization tank and rotates to stir the household wastes in the carbonization tank. When the household waste is stirred, the household waste can be brought into contact with or near the ceramic layer for far-infrared radiation coated on the inner wall of the carbonization tank, and this makes it possible to efficiently irradiate the infrared with the household waste. As a result, dry, thermal decomposition, and carbonization of household waste can be uniformly, efficiently and quickly. Carbide remaining in the lower part or side of the carbonization tank can be taken out from the inlet installed in the lower part of the carbonization tank.

Far-infrared radiation ceramic coatings that emit a wide range of high-efficiency far-infrared rays are simple operations that are applied to the inner wall of the carbonization tank and then naturally dried, and can be easily painted. As a result, the manufacturing cost of the carbonization tank formed with the far-infrared radiation ceramic layer can be reduced compared to the previously known method, and the economic value is generated.

As a heating means, the electric heater is a ceramic insulator having a cylindrical body divided into two, and heat wires such as nichrome wire heaters and canal wire heaters are provided in the inner grooves thereof. The cylindrical electric heater is disposed so as to embrace the outer side of the carbonization tank, and the far infrared radiation ceramic layer coated on the inner surface of the carbonization tank and the carbonization tank is radiated by the electric heater. When gas or petroleum is used as the heat source, the combustion gas of this gas or petroleum is introduced to the outside of the carbonization tank in a suitable manner, and the heat of the far-infrared radiation-emitting ceramic layer and the carbide are heated by the combustion gas heat.

1 is a partial cross-sectional view for explaining the apparatus according to the present invention,

FIG. 2 is an enlarged view of only the carbonization tank and the heating unit in FIG. 1;

3 is a cross-sectional perspective view showing only the heating unit separately;

4 is an enlarged plan view of a pressure plate separated from FIG. 1.

* Description of the symbols for the main parts of the drawings *

10: main body case 20: carbonization processing unit

23: carbonization tank 26: ceramic layer for far infrared radiation

21: first heating heater 30: carbide moisture treatment unit

36: water reservoir 37: second heater for heating

40: stirring device 41: stirring blade

50: exhaust gas treatment unit 54: third heating heater

57a to 57c: first to third catalysts 58: blower

59: vacuum pump 70: far infrared radiation honey kam heater

80: water tank 82: air bubble generator

84: ion stone

Hereinafter, a more preferred embodiment of the waste carbonization device according to the present invention will be described in detail with reference to the accompanying drawings.

1 is a partial cross-sectional view showing the whole of the apparatus according to the present invention, Figure 2 is a cross-sectional view of the carbonization tank, Figure 3 is a heating unit for heating the carbonization tank, Figure 4 is an enlarged view showing only the pressure plate in FIG. Top view.

In FIGS. 1-3, the code | symbol 10 is a main body case. The upper part of the main body case 10 is opened, and the opening is sealed by the case cover 12.

Reference numeral 23 is a carbonization combination combined in the main body case 10, the upper portion (case cover: 12) is formed with a carbide inlet 14, the lower portion is formed with a carbide outlet 15, the inner surface As shown in Fig. 1 and Fig. 2, a far-infrared radiation-emitting ceramic layer 26 exhibiting heat resistance even at a high temperature of about 1000 ° C is formed on the whole.

Reference numeral 27 is a heating unit (UNIT) provided to surround the outer portion of the body of the carbonization tank 23, as shown in Figures 2 and 3, the heating unit 27 is a ceramic insulator 28 The heater accommodating groove 29 is formed in the inner surface of the c), and the first heating heater 21 is incorporated into the heater accommodating groove 29. As the first heating heater 21, a nichrome wire, a canal wire heater, or the like is used. However, the above example is not limited, and any suitable heat transfer heater material can be used. As the heating unit 27, in addition to the first heating heater 21 of the embodiment, a combustion gas heater such as gas or oil can be used. The above components constitute the carbonization processor 20 of FIG. 1.

Reference numeral 30 is a pre-carbide, for example, for the rapid carbonization of carbonized carbides, for example, household wastes and industrial wastes, which are contained in the carbonization tank 23 of the carbonization processing unit 20 through the inlet 14. Carbide moisture treatment unit used to discharge moisture into the air. The carbide water treatment unit 30 includes a pressure plate 33 for pressing the carbides introduced into the carbonization tank 23. As shown in FIG. 4, the pressure plate 33 may cut a portion of the plated carbide to be inserted into the carbonization tank 23 so that the carbide is introduced into the carbonization tank 23. A wide range of carbide inputs 35 can be formed. The shape of the carbide input unit 35 may be any shape as long as possible to insert the carbide easily. The pressure plate 33 is loosely coupled to the pressure plate 33 and at least two screw rods 32a and 32b which are movably penetrated in the state penetrating the case cover 12 include the case cover 12. Pressurized carbide is moved upwards and downwards depending on whether or not the stepping motors 31a and 31b are engaged with the electric gears 34a and 34b with respect to each of the screw rods 32a and 32b on an upper surface thereof. By doing so, moisture contained in the carbide is discharged. Since the screw rods 32a and 32b are loosely coupled to the pressure plate 33, the screw rods 32a and 32b are rotated freely regardless of the pressure plate 33, thereby allowing the pressure plate 33 to move. Allow to descend or rise. In addition, the lowering distance of the pressure plate 33 is preferably to be moved only to a distance that does not touch the stirring blade 41 of the stirring device 40 to be described later. This movement distance can be set by the driving adjustment of the stepping motors 31a and 31b. Since this is a general technology, a detailed description thereof will be omitted.

Water discharged from the carbide to be pressurized by the pressure plate 33 is in contact with the carbonization tank 23 and the distribution passage 38 at the bottom of the carbonization treatment unit 20 is installed in the water reservoir 36 Gathered inside). At the inlet of the flow passage 38, it is preferable to install the filtering net 39 to filter foreign matter contained in the water discharged from the carbide. Moisture collected in the water reservoir 36 through the filter net 39 is evaporated while being heated by a second heating heater 37 which is disposed directly below the water reservoir 36. The stepping motors 31a and 31b and the second heating heater 37 are controlled while being collectively turned on / off in the control panel 60 in which the CPU control circuit is incorporated.

Reference numeral 40 is a stirring device, the stirring blade 41 put upward from the lower center in the carbonization tank 23, the base of the rotating shaft 42 is detachable to the connector 43, For example, it is used to remove the waste sheet when it is not needed, to mount it in the case of household waste, to stir, and to irradiate the household waste with far-infrared rays and heat evenly to increase the far-infrared effect and carbonization.

Reference numeral 44 denotes a stirring motor that allows the stirring blade 41 to rotate via the connector 43, and an inverter-type variable speed motor is used. However, the inverter variable speed motor is an example, and other known variable speed motors can be used.

Reference numeral 50 denotes an exhaust treatment unit, and an exhaust pipe 56 that extends outwardly of the main body case 10 is installed from an exhaust port 55 formed in an upper portion (case cover) 12 of the carbonization tank 23. It is. The exhaust pipe 56 is preferably made of a stainless steel plate having corrosion resistance, and the shape of the exhaust pipe 56 is preferably configured to rotate in a spring shape about 2.5 times. The first inlet portion of the exhaust pipe 56 is provided with a condenser 51 for the purpose of removing water vapor generated when far-infrared carbonization.

After the condenser 51, a first catalyst 57a is installed, and the first catalyst 57a is capable of removing dust, i.e., floating oil fine particles, and the like. Is oxidized in the first catalyst 57a by the internal temperature (250 ° C.) of the carbonization tank 23.

After the first catalyst 57a, a second catalyst 57b is provided, and the odor is removed using a known oxidizing catalyst for treating the exhaust gas containing the untreated organic matter mixed in the first catalyst 57a. To be removed. The second catalyst 57b is a catalyst obtained by coating a noble metal (Pt, Pd) on a honeycomb carrier.

After the second catalyst 57b, a third catalyst 57c is provided to use dioxins in the exhaust gas which cannot be treated by the first catalyst 57a and the second catalyst 57b using a known oxidation catalyst. It was possible to complete the process.

Reference numeral 53 is an oxygen supply pipe having a substantially '대략' shape, and is preferably installed in the middle portion of the third heating heater 54 which will be described later. In addition, the supply of oxygen is preferably supplied only 5 to 10% of the total organic content, the operation is supplied to the oxygen for approximately 50 minutes after the operation, after 50 minutes automatically stops the operation, this control of the operation It is controlled from the control panel 60.

The third heating heater 54 is configured in a coil shape, and is a catalyst heating heater for oxidizing degradable organic substances to the second catalyst 57b and the third catalyst 57c, wherein the second catalyst 57b The heating temperature is preferably 350 ± 10 ° C., and the heating temperature of the third catalyst 57c is within 220 ± 5 ° C. The control of the third heating heater 54 for heating the second catalyst 57b and the third catalyst 57c is executed by the control panel 60.

Reference numeral 52 is a cooling fan. The exhaust gas flowing through the exhaust pipe 56 via the catalysts has a temperature difference depending on the type of waste carbonized, but the exhaust gas is disposed at the exhaust pipe 56 at a high temperature of approximately 100 to 130 ° C. The blower 58 and the vacuum pump 59 and the like cause failure due to high temperature gas. In order to prevent this in advance, the high temperature exhaust gas passing through the exhaust pipe 56 as the cooling fan 52 is prevented. It is desirable to cool the C to fall below a predetermined temperature.

The exhaust gas passing through the exhaust pipe 56 is cooled by the cooling fan 52, but since it has heat to some extent, smooth exhaust may not be performed properly. Therefore, in order to smoothly flow the exhaust gas, it is necessary to forcibly exhaust the inside of the exhaust gas cylinder 59a installed in contact with the blower 58 via the blower 58 provided in the exhaust pipe 56.

Reference numeral 59 denotes a vacuum pump, which is installed to be in contact with the exhaust gas cylinder 59a and sucks the exhaust gas concentrated in the exhaust gas cylinder 59a to communicate with the vacuum pump 59. It is discharged to be introduced into the water tank 80 which will be described later. The inside of the exhaust gas cylinder 59a is made into a vacuum atmosphere by the vacuum pump 59. The vacuum pump 59 discharges exhaust gas by the amount of exhaust gas flowing into the water tank 80.

The water tank 80 is filled with water, and the air bubble generator 82 installed at the tip of the tube 86 extending from the vacuum pump 59 is installed in the water tank 80. By placing the ionic stone 84 on the upper portion, the gas discharged by the vacuum pump 59 is dispersed by the air bubble generator 82 and adsorbed to the negative ionic stone 84. It finally ionizes and removes the substances that cause environmental deterioration and dissipates them into the atmosphere.

Reference numeral 60 denotes a control panel, which includes a temperature controller 61 for controlling the temperature of the heating heaters 21, 37, and 54, and a moving speed and stirring blades of the pressure plate 33. An agitation speed controller 62 for controlling the rotation speed of the 41 and the like is provided, and although not shown in the drawing, the control panel 60 includes an oxygen supply pipe 53, a cooling fan 52, and a blower 58. Necessary circuit diagrams such as a circuit for driving the vacuum pump 59 and the like, such as an overheat prevention circuit and a performance monitoring circuit of the first to third catalysts 57a to 57c, are included therein.

Reference numeral 73 denotes a far-infrared radiation honeycomb heater mounting hole used when the stirring blade 41 is removed from the carbonization tank 23, and a salt sheet is added to the inside to carbonize the far-infrared radiation honeycomb heater. The mounting hole 73 is coated with a honeycomb-like far-infrared radiation coating material, and the hot air generated by the electric heater 72 at the rear is passed through the honeycomb-shaped carrier 74. In the carbonization tank 23, a far-infrared radiation honeycomb heater 70 for radiating far-infrared rays and hot air to enable carbonization of carbides is provided. The far-infrared radiation honeycomb heater 70 can also be used in the treatment of household waste, and at this time, it can be used together with the heating unit 27 on the carbonization tank 23 side. Of course, this combination can be used also for the waste disposal of a vinyl salt sheet plastic. In addition, the far infrared honeycomb heater 70 includes a heater calcined with a material containing a far infrared ray ceramic.

In order to process household waste, the stirring blade 41 is formed on the inner wall of the carbonization tank 23 to form a ceramic layer 26 for far-infrared radiation, and the stirring blade 41 is kept in the closed state of the carbonization tank 23. By heating the first waste heater 21 disposed outside the carbonization tank 23 while stirring the household wastes well, and thermally decomposing and carbonizing the waste while efficiently drying the household waste by the heating and far-infrared radiation. have.

According to the above embodiment, when the far-infrared radiation ceramic layer 26 is coated on the inner wall of the large carbonization tank 23, the heat-resistant far-infrared radiation ceramic at 1000 ° C. is painted at room temperature and naturally dried at room temperature, and does not require a ignition process. Since it can be painted without, the large carbonization tank 23 having the far-infrared radiation ceramic layer 26 on the inner wall can be easily manufactured at low cost.

In the case of processing vinyl sheets, the stirring blade 41 of the carbonization tank 23 which processes household wastes has a large volume of vinyl sheets, and is difficult to use because it is entangled with the stirring blades 41. In this case, a honeycomb type far-infrared radiation heater 70 of the carbonization tank 23 is installed so that far-infrared rays are radiated to the plastic sheets at the top and carbonized together. By heating with the 1st heating heater 21 by the side of the tank 23, the vinyl sheets injected into the carbonization tank 23 by this heat and far-infrared radiation heat are thermally decomposed and finally carbonized and annihilated.

Moisture generated when drying and carbonizing the household wastes and vinyl sheets is condensed and treated as the condenser 51, and then dust, that is, floating oil fine particles and the like is oxidized by the first catalyst 57a. Hazardous gases such as carbon monoxide, which are not filtered out of the first catalyst 57a, are removed from the second catalyst 57b, and the third catalyst 57c completely oxidizes hardly decomposable organic substances such as dioxin and carbon dioxide gas, Disintegrates into inorganic materials such as water and chlorine.

(1) In the case of household garbage

A large amount of household wastes are introduced into the carbonization tank 23 coated with the far-infrared ray-proof ceramic layer 26 at the inlet 14, and then the water is discharged by the carbide moisture treatment unit 30 to thereby discharge the second heating heater 37. As evaporated. The household wastes treated with the stirring blade 41 are well stirred, and the household wastes are brought into contact with or in close proximity to the far-infrared radiation-coated ceramic layer 26 coated on the inner wall of the carbonization tank 23. The carbonization tank 23 is heated by the heating unit 27 disposed outside the carbonization tank 23, and the household waste is heated. At the same time, the far-infrared radiation ceramic layer 26 painted on the inner surface of the carbonization tank 23 is heated and radiated far-infrared rays are irradiated to the household waste, and the household waste is efficiently dried, thermally decomposed and finally carbonized. . When the household waste is carbonized, dust among the evaporated components generated is removed by the first catalyst 57a, and harmful gases such as carbon monoxide are released by the second catalyst 57b.

(2) In the case of plastic waste such as vinyl sheets

Since it is difficult to agitate the agricultural vinyl sheet with the stirring device, the stirring blade 41 of the present device is removed, and the agricultural vinyl sheet is introduced into the inlet 14. By heating the honeycomb-type far-infrared radiation heater 24 of the carbonization tank 23 to radiate far infrared rays, the carbonization tank 23 in the first heating heater 21 which is a heating unit 27 outside the carbonization tank 23. And heating the far-infrared radiation ceramic layer 26 coated on the inner wall of the carbonization tank 23 at the same time, by emitting far-infrared radiation from the far-infrared radiation ceramic layer 26 to a vinyl sheet, etc. Pyrolyzed and carbonized. Dust such as floating oil fine particles generated by carbonization operation is removed by the first catalyst 57a, and harmful gases such as carbon monoxide are removed by the second catalyst 17b, and hardly decomposable organic substances such as dioxins are produced by the third catalyst. It is completely oxidized by the catalyst 17c and oxidized to inorganic matter. In particular, the filtration by the catalysts is more effectively treated by the air supplied from the oxygen supply pipe 51 and the temperature heated by the heating heater 54. The inorganicized evaporated component is cooled by the cooling fan 52 and then introduced into the water tank 80 by the blower 58, the exhaust gas cylinder 59, the vacuum pump 59, and the air bubble generator 82. It is ionized through the ion stone 84 and then dissipated.

<Operation example>

(1) carbon waste treatment

• The carbonization tank 23 and the far infrared ray ceramic layer 26 are heated at a heating temperature of 400 to 300 ° C.

ㆍ stirring speed 200 ~ 500rpm

(2) Carbonization of plastics such as vinyl sheets

(1) The carbonization tank 23 and the far infrared ray ceramic layer 26 are heated at a heating temperature of 400 to 300 ° C. It heats with the far infrared ray ceramic heater 70 arrange | positioned at the head at the heating temperature of 400-300 degreeC.

② The carbonization tank 23 and the far infrared ray ceramic layer 26 are heated at a heating temperature of 400 to 300 ° C. It heats with the far-infrared radiation ceramic heater 70 arrange | positioned at the head at heating temperature 400-300 degreeC. In this case, plastics are oxidized after carbonization and become inorganic substances such as carbon dioxide (CO ₂ ) and water vapor (H ₂ O).

ㆍ First catalyst device 57a

<Formula 1>

200 ~ 400 ℃

(HC) + AlR (O ₂ ) → CO ₂ + H ₂ O

Hydrocarbon catalyst

ㆍ second catalyst device 57b

The evaporated component generated after the carbonization treatment is oxidized in the second catalyst device 57b.

It heats to 350 degreeC or more by the heater for a catalyst.

<Formula 2>

350 ℃

CmHn + O ₂ → CO ₂ + H ₂ O

Hydrocarbon Oxygen Catalyst Carbon Dioxide Water

(Low Molecular Organics) (Carbon Gas)

350 ℃

(CH ₃ ) ₃ N + O ₂ → CO ₂ + H ₂ O + N ₂

Trimethylalmine oxygen carbon dioxide water nitrogen

Carbon dioxide

350 ℃

(NH ₃ ) + O ₂ → N ₂ + H ₂ O

Ammonia Oxygen Catalyst Nitrogen Water

<Formula 3>

ㆍ 3rd catalyst device (57c)

Example of Decomposition of Dioxin (PCDD)

2,3,7,8tetrachlorojibenzozicin oxygen catalyst carbon dioxide water chlorine

(PCDD)

(Dioxin) oxygen carbon dioxide

Hardly degradable organics

Plastic waste treatment devices such as household waste and salty sheets according to the present invention are heated by using a heating source such as an electric heater, gas, oil, etc., after being treated with water, and radiated by the far-infrared radiation ceramic coated on the inner wall of the carbonization tank. The material is uniformly agitated with a stirring device installed inside the carbonization tank so as to dry, dry, and thermally decompose the object by using far infrared rays, and at the same time, evenly irradiate the object with even infrared rays. By moving and contacting or proximity of water to the far-infrared radiation ceramic layer, the treated water can be dried, pyrolyzed and carbonized more quickly, completely and efficiently. As a result, the present invention has the following effects.

1. It is possible to easily form a far-infrared radiation-proof ceramic layer in a carbonization tank without applying a high efficiency far-infrared radiation ceramic paint to the inner wall surface of the carbonization tank, and only baking it naturally. As a result, manufacturing cost for forming a far infrared ray ceramic layer on the inner surface of the carbonization tank can be saved.

2. The water to be treated can be treated beforehand, so that the carbonization time can be reduced and the fuel consumption can be reduced accordingly.

3. It is possible to save the price of heat source by using far-infrared radiation ceramic to use electric heater, gas and oil alone as heat source.

4. Far-infrared radiation Because it is easy to paint ceramic paint, the area of far-infrared radiation can be made large.

5. Smoke, odor, low molecular organic matter and hardly decomposable organic substances generated by carbonization of treated materials are completely oxidized to inorganic substances by catalyst device, preventing odor pollution and harmlessness, and used for business and industrial purposes. Can be.

6. By using the far-infrared radiation ceramic layer and the stirring device, the center of the workpiece can be brought into contact with and in close proximity to the far-infrared radiation ceramic layer by stirring, so that the workpiece can be uniformly dried completely and carbonized. In addition, processing time can be shortened.

7. This design is used for high throughput business, but can also be enlarged for industrial use. If necessary, it can be miniaturized and used for general homes and ships.

8. The air bubble generator can dissolve the exhaust gas in water faster and treat it, and ionize it with ionic stone to make it more environmentally friendly.

Claims (8)

In the waste carbonization apparatus, A carbonization treatment unit which forms a heat-resistant far-infrared radiation ceramic layer on the inner wall surface of the carbonization tank in which waste is accommodated and at the same time installs a first heating heater on the outer side of the far-infrared radiation ceramic layer; Pressing means is installed to move up and down from the upper portion of the carbonization treatment portion and pressurized to discharge the water contained in the carbonization tank during the downward movement, through the carbonization tank and the filter net at the bottom of the carbonization treatment portion facing the pressing means Carbide moisture treatment unit is installed in contact with the water storage container for storing the water discharged from the carbonization waste and the second heating heater disposed under the water storage container directly to apply heat; A stirring device which is driven by a motor installed in the carbonization tank to agitate the carbonated material dehydrated in the carbide water treatment unit and freely detachable from the motor in the carbonization tank; The inside and outside of the carbonization tank is installed to be in contact with the upper part of the carbonization tank in which the stirring device is installed to remove dust, odor and smoke components in the exhaust gas discharged from the carbonization tank, and to remove odor and smoke. Exhaust treatment for i); and And a water tank at the final stage of the exhaust treatment unit includes a water tank which finally introduces and treats exhaust gas into water to remove environmental pollutants such as smoke. The head of the carbonization tank is further provided with a honeycomb-type far-infrared radiation heater, so that carbonization can be performed alone or in combination with a far-infrared radiation ceramic layer on the object in the carbonization tank. Waste carbonization apparatus, characterized in that. The waste carbonization apparatus according to claim 1, wherein the heat-resistant far-infrared radiation ceramic layer is formed by applying a far-infrared radiation ceramic coating to the inner surface of the carbonization tank. According to claim 1, wherein the pressing means presses the carbides introduced into the inside of the carbonization tank, the pressure plate is formed in the injection portion, the part is loosely coupled to the pressing plate 2 is installed so as to move through the case cover And two screw rods, stepping motors mating through the electric gears with respect to each of the screw rods on the upper surface of the carbonization tank. According to claim 1, wherein said exhaust treatment unit discharge pipe which is in contact with the outside from the carbonization tank; And And a first catalyst and a third catalyst installed in order to contact the discharge pipe in order to remove odor, dust, carbon monoxide, dioxin, and the like from the fumes discharged from the carbonization tank. The water tank of claim 1, wherein the water tank is operated by a vacuum pump for sucking exhaust gas into the water tank, and an ion stone for anion treating water flowing together with the gas discharged from the air bubbler. Waste carbonization apparatus characterized in that it is further provided. 6. The catalyst according to claim 1 or 5, wherein a condenser for removing water generated from the carbides in the carbonization tank and a catalyst for treating the exhaust gas through the condenser are located at an adjacent portion of the exhaust treatment unit with the catalysts. And a third heating heater for heating them. The cooling fan or blower according to claim 1 or 5, wherein the exhaust pipe of the exhaust treatment unit is arranged to be in contact with each other between the catalyst and the water tank to smoothly discharge the exhaust gas via the exhaust pipe. And an exhaust bin.