JP3109984U - Garbage disposal device - Google Patents

Abstract

Disclosed is a new and improved garbage disposal device that is free from air pollution due to sewage contamination and heat extinction, and that can effectively achieve a treatment time and a weight reduction effect.
A crushing function unit for crushing raw garbage by a stirring blade of a stirring impeller having an inlet 112 for putting the raw garbage into a reaction chamber and a heating means 120 for heating the raw garbage to generate water vapor. 140 is formed, the condenser 200 that condenses the garbage in the reaction tank, and the air that has passed through the condenser smells while passing through the ceramic carrier and the multiple platinum catalyst layers by the heat energy of the electric heater. It is configured to include a deodorizer 300 to be removed and discharged, a blower that pumps the air that has passed through the condenser 200 to the deodorizer 300, and an automatic drain pipe 500 that filters the condensed water generated from the condenser 200. Characteristic garbage disposal equipment.
[Selection] Figure 1

Description

  The present invention relates to a garbage disposal device. More specifically, the present invention relates to a garbage disposal device that achieves the goal of weight reduction and reduction by rapidly drying and decomposing food waste by indirect heating with heat transfer oil.

  Conventional garbage disposal methods include various methods such as fermentation, fermentation extinguishing, screw press dewatering, piston press dewatering, dewatering drum rotary centrifugal dewatering, heat drying, and incineration. However, the fermentation method and the fermentation extinction method are non-hygienic methods that use microorganisms, and have a larger machine, more installation space, higher cost, and longer processing time than the processing capacity. It is inconvenient to use because it is difficult to manage microorganisms and causes environmental pollution due to the generation of intense odor during fermentation.

  In addition, sewage contamination due to squeezing and dewatering is serious in the squeezing methods such as the screw squeezing method and piston squeezing method, and it is difficult to remove the residue remaining on the dewatering filter and to perform cleaning and sanitary treatment, and additional odor due to spoilage occurs. Therefore, it is inconvenient to use because the solution of these problems is not easy, the water content of the treated product is high, and the weight loss rate is low.

  In addition, the spin-drying centrifugal dewatering type has the advantages of quick processing time and low energy consumption, but it is not easy to remove debris remaining in the dewatering holes and clean it. The treated product has a high moisture content, a low weight loss rate, and a secondary treatment is required. If it is not managed, there is a disadvantage of causing environmental pollution due to the occurrence of rot and odor.

  In addition, the heat drying method uses electricity and fuel, so energy consumption is large for hot air drying, and severe odors are generated. Life is short.

  Also, the incineration type fires the treated material directly, so large gases and incomplete combustion due to low calorific value generate dioxins and other harmful gases, consuming large amounts of energy, and ensuring the safety of the equipment. There is a problem in use because it greatly affects the surrounding environment.

  Therefore, the present invention has been made in view of such problems. The purpose of the present invention is to grind and squeeze the garbage while forcedly dewatering it and drying it while dispersing it with a stirrer. The crushing function unit breaks down into small pieces, passes the steam through the condenser, discharges only pure substances to the outside, and adopts an air circulation inflow method that enters the reaction tank again and discharges it to the outside. It is a new and effective way to achieve the treatment time and weight reduction effect by eliminating the air to be used, almost no heat loss, no bad smell, no pollution of sewage by artificial forced dehydration and no air pollution by heat incineration, etc. The object is to provide an improved garbage disposal device.

  Another object of the present invention is that the heat energy is very low in energy consumption, has few failure elements, and is safe by using a stepped electric heater method and efficient operation. To provide a new and improved garbage disposal system that can be installed in a low cost and can be widely used because installation space and operating costs can be saved, so there is almost no maintenance cost that has been burdened so far. It is in.

  In order to achieve such an object, the feature of the present invention is that the top and side surfaces of a hopper having a reaction chamber sealed inside are respectively an inlet for allowing the garbage to flow into the reaction chamber, and the treated garbage. A discharge port for discharging from the reaction chamber is formed so as to be openable and closable by a lid, and a heating means for heating raw garbage put into the reaction chamber to generate water vapor is provided at the lower part of the hopper. An agitation impeller that stirs and disperses garbage in the chamber and collects it in one place is rotated by a drive motor. On the inner surface of the reaction chamber, garbage agitated by a stirring blade is placed. A reaction tank in which a crushing function part to be crushed is formed; and a plurality of support frames each having a hole part in the interior thereof, so that the cooling pipe communicates with the hole part. In addition, a cooling fan that blows cool air is installed in the part adjacent to each pipe, an automatic drain pipe is formed in the lower part of the support frame, and the one side support frame is formed by a reaction tank hopper and a connecting pipe. Water vapor generated while food waste is heated in the reaction tank is connected to communicate with the cold air through the connecting pipe and the cooling pipe, and is separated into water and air. The heat supply pipe having a guide hole in the interior thereof and the catalyst pipe are formed so as to communicate with each other, and a heat dissipating heater with blades attached to the inside of the heat supply pipe is fixedly disposed. Inside, the ceramic carrier for preventing heat aging and a large number of platinum catalyst layers are fixed and arranged at appropriate intervals, and the heat supply pipe is connected so as to communicate with the other support frame of the condenser through the connecting pipe, Is connected so as to communicate with the reaction vessel hopper through a connecting pipe, and a cooling discharge pipe is connected on the connecting tube connected so that the catalyst pipe and the reaction vessel hopper communicate with each other. A deodorizer configured to perform deodorization while the air passing through the apparatus passes through the heat supply pipe and the catalyst pipe; an input pipe in which the air having passed through the deodorizer is re-supplied in the reaction tank and an internal air pressure load A discharge pipe connected so as to discharge to the outside depending on the volume; a blower installed on a connection pipe connecting the condenser and the deodorizer, and sending the internal air passing through the condenser to the deodorizer; and a support frame of the condenser A large number of fibrous activated carbons are arranged in a stack inside the automatic drain pipe connected to communicate with the drain cock formed at the bottom of the pipe, and a water pipe is formed under the drain cylinder. The condensation generated from the condenser Wastewater treatment characterized by having a drain pipe connected to a drain pipe connected to the lower side of the automatic drain pipe and drained as pure material under the automatic drain pipe while the condensed water passes through the activated carbon layer A vessel is provided.

  As described above, the garbage processing apparatus according to the present invention generates steam while the garbage is crushed and dried in the reaction tank, and the condenser condenses the steam generated in the reaction tank to produce water. In the deodorizer, the air separated from the condenser is deodorized and then re-supplied to the reaction tank. In the activated carbon filter, the extraneous matter condensed in the condenser is finally filtered to the outside. While the discharge process is continuously repeated for the set time, the raw garbage that was initially put into the reaction vessel is completely dried and decomposed and remains in the powder form. The treatment is more hygienic and has the effect of reducing the amount quickly.

  In addition, the garbage disposal device according to the present invention operates with less energy because a heater, which is a heating means for heating and drying the garbage thrown into the reaction chamber of the reaction tank, is heated by a stepped electric supply system. The air circulation re-inflow method eliminates the air that is re-introduced into the reaction tank and discharged outside during operation, and there is no odor and heat loss. It has the effect of saving costs and solves the fundamental problems.

  In addition, the garbage disposal device according to the present invention is agitated while the garbage introduced into the reaction chamber of the reaction tank is uniformly dispersed by the agitating blades when it is rotated in the forward direction of the agitation impeller and dried by the heating means. At the same time, when the stirring impeller rotates in the opposite direction, it is gathered in the center by the stirring blades, and the processed garbage in the form of powder can be discharged smoothly through the discharge port, so that the equipment can be used conveniently.

  Exemplary embodiments of the present invention will be described below in detail with reference to the accompanying drawings. In the present specification and drawings, components having substantially the same functional configuration are denoted by the same reference numerals, and redundant description is omitted.

  First, a garbage disposal apparatus according to an embodiment of the present invention will be described. FIG. 1 is an overall configuration diagram showing a garbage disposal device according to an embodiment of the present invention, FIG. 2 is a side sectional view of a reaction tank which is a main part of the garbage disposal device according to the present invention, and FIG. FIG. 4 is a perspective view showing an agitation impeller as a main part of a garbage disposal device according to the present invention, and FIG. 4 is a configuration diagram showing an electric control unit of the garbage disposal device according to the present invention.

  The garbage processor according to the present invention includes an inlet 112 through which the garbage is introduced into the reaction chamber 111 on the top and side surfaces of the hopper 110 having the reaction chamber 111 sealed inside, and the treated garbage in the reaction chamber 111. A discharge port 113 for discharging from the reaction chamber 111 is formed so as to be openable and closable by a lid, and a heating unit 120 for generating steam by heating raw garbage input from the reaction chamber 111 is provided below the hopper 110. A stirring impeller 130 that stirs and disperses garbage or collects it in one place is installed in a reaction chamber 111 of 110 so as to be rotated by a driving motor 150, and the stirring impeller 130 and the driving motor 150 are connected to each other. A chain adjustment gear 154 for adjusting the chain tension is attached to the chain. The reaction chamber 100 is formed with a crushing function unit 140 for crushing raw garbage agitated by the agitation impeller 130 on the inner side surface of the reaction chamber 111; and a plurality of support frames 210 having inside holes 211 therein. The cooling pipe 220 is connected so as to communicate with the middle hole portion 211 therebetween, and a cooling fan 230 that cools the cooling pipe 220 by blowing cold air is installed at a portion adjacent to each pipe 220 to support the cooling pipe 220. An automatic drain pipe 500 is formed in the lower part of the frame 210, and the one-side support frame 210 is connected so as to communicate with the hopper 110 of the reaction tank 100 by the connection pipe 240, and the garbage is heated in the reaction tank 100. The water vapor generated while passing through the connecting pipe 240 passes through the support frame 210 and the cooling pipe 220 and contacts cold air. Then, when condensed, the condenser 200 separates into water and air; a heat supply pipe 310 having a guide hole 311 therein and a catalyst pipe 320 are formed so as to communicate with each other. An electric heater 330 is fixedly arranged, a ceramic carrier 350 for preventing heat aging and a large number of platinum catalyst layers 340 are fixedly arranged at appropriate intervals inside the catalyst tube 320, and the heat supply pipe 310 is connected to the condenser 200. The catalyst tube 320 is connected so as to communicate with the other side support frame 210 via the connecting tube 360, and the catalyst tube 320 is connected so as to communicate with the hopper 110 of the reaction vessel 100 via the connecting tube 370, so that the catalyst tube 320 and the hopper 110 of the reaction vessel 100 are connected. The cooling exhaust pipe 380 is connected on the connecting pipe 370 connected so as to communicate with each other, and the air passing through the condenser 200 is sent by the blower 400. The deodorizer 300 is deodorized while passing through the electric heater 330 of the heat supply pipe 310 and the platinum catalyst layer 340 of the catalyst pipe 320; the condenser 200 is installed on the connecting pipe 360 connecting the deodorizer 300 to the condenser 200. A blower 400 that pumps air discharged from the deodorizer 300; a number of fibrous activated carbons inside a drain cylinder 510 that is connected so as to communicate with a drain cock 212 formed at a lower portion of a support frame 210 of the condenser 200 The layer 520 is disposed in a stack, and a drain pipe 530 is formed to communicate with the lower side of the drain cylinder 510. Condensed water generated in the condenser 200 passes through the fibrous activated carbon layer 520, and finally It consists of an automatic drain tube 500 that is filtered and discharged.

  As shown in FIGS. 2 and 3, the stirring impeller 130 of the reaction vessel 100 is horizontally disposed in the reaction chamber 111 of the hopper 110 so as to be rotatable about the shaft shaft 131, and a number of stirring blades are disposed on the shaft shaft 131. 132 is configured to be fixedly coupled in a radial manner with a predetermined interval around the shaft axis 131 by the pivot arm 133. Also, a soup racket 152 is fixedly coupled to the shaft shaft 131 and the driving shaft 151 of the driving motor 150, and the soup racket 152 is coupled so as to be interlocked with the chain 153. The drive of the drive motor 150 is controlled by the electric control unit 600 according to the time during which the garbage is processed in the reaction tank 100.

  As shown in FIG. 3, the stirring blade 132 is configured such that the stirring piece 132A for pushing and stirring the garbage and the inclined piece 132B are integrally coupled to the back surface of the stirring piece 132A so as to be inclined at a constant angle. When the inclined pieces 132B are symmetrically installed around the intermediate portion of the shaft shaft 131 and the shaft shaft 131 rotates in the forward direction, the garbage is uniformly distributed in the direction of both ends of the shaft shaft 131 by the stirring pieces 132A of the stirring blades 132. When the shaft shaft 131 rotates in the opposite direction after being dispersed and stirred, the garbage is collected in the center of the reaction chamber 111 while being pushed by the inclined piece 132B of the stirring blade 132, and the solid matter processed at this time Is discharged from the reaction chamber 111 at an intermediate portion of the shaft shaft 131 where garbage is collected by the stirring blade 132. It made it is preferable.

  Further, the crushing function unit 140 fixedly coupled to the stirring blade 132 of the stirring impeller 130 and the inner wall of the reaction chamber 111 of the hopper 110 is installed so as to be adjacent to each other as shown in FIG. It is comprised so that it can cut | disconnect and crush between between the stirring blade 132 and the crushing function part 140 to be performed.

  The heating means 120 which is a double cylinder includes a heating frame 121 having a heating chamber 121A therein and is integrally formed so as to partially wrap the lower and side surfaces of the hopper 110, and the heating frame 121 is electrically heated. The heat medium oil 123 is stored in the heating chamber 121A so that the heat medium oil 123 is heated by the heater 122, and the hopper 110 is heated by the heat medium oil 123 so that the heat medium oil 123 is heated. Is configured to heat indirectly.

  The heating heater 122 of the heating means 120 supplies the power consumption capacity supplied by the stepped electric supply system to the maximum initial installation strength during operation, and heats the heat transfer medium oil 123 quickly, so that the inside of the reaction chamber 111 Then, the power consumption capacity supplied by the heater 122 is increased (the heat medium oil 123 has already risen in temperature and requires a conduction time into the reaction chamber 111). About half (about 1/2) is supplied and heated until the temperature in the reaction chamber 111 is conducted at about 80 ° C. After that, when the temperature in the reaction chamber 111 reaches about 80 ° C., the heating of the heat medium oil 123 is performed. The power consumption capacity supplied to the heater 122 is supplied to about 1/4 of the initial installed strength so that the operating temperature of about 80 ° C. in the reaction chamber 111 can be maintained continuously. By operating the electrical energy supplied to the heater until the end of work only with minimum power consumption, and a step electric supply system to minimize power consumption.

  From the experimental results, the power consumption capacity of the staged power supply system is initially 4kW, the installed strength, is supplied for about 30 minutes, then it is lowered to 2kW for about 20 minutes, and finally the power consumption capacity of 1kW. Is configured to be supplied until the end of the work.

  A temperature detection sensor 160 is installed in the hopper 110 of the reaction tank 100, and the operation of the heater 122 is controlled by the controller according to a signal from the temperature detection sensor 160. Is provided with a heat medium auxiliary tank 170. When the heat medium oil 123 in the heating means 120 undergoes thermal expansion by the heater 122, the heat medium auxiliary tank 170 rises up to a certain pressure or higher, and an expansion valve 171 is set. It is configured to be automatically opened and closed so that the internal pressure is discharged to the outside. At this time, the heating means 120 is connected to communicate with the heat medium auxiliary tank 170.

  A large number of cooling blades 221 are formed at both ends of each cooling pipe 220 of the condenser 200, and the condensation of water vapor through the cooling pipe 220 is performed more efficiently by increasing the contact area with the outside. The platinum catalyst layer 340 of the deodorizer 300 is configured by coating platinum on a honeycomb-shaped ceramic surface.

  The drive motor 150 is capable of forward and reverse rotation, and the chain 153 that transmits the driving force of the drive motor 150 by the stirring impeller 130 is configured so that the tension is maintained by the chain adjustment gear 154. In addition, a large number of radiating blades 331 are formed in the electric heater 330 of the deodorizer 300, and the internal air entering the blower 400 is heated by the electric heater 330 by increasing the contact area with the outside, and the heat supply pipe It is designed and configured to move to the catalyst tube 320 while maintaining the temperature in 310 at an appropriate temperature.

  The electric control unit 600 has an operation time operation panel 601 and a failure lamp 602 for notifying a failure during overheating and overloading or notifying that the machine is stopped. A power switch 603 is used for receiving primary incoming electricity. When the operation switch 604 is pressed with the switch, all functions are automatically controlled until the work is completed. When the discharge switch 605 is pressed, the final by-product is discharged to the outside. When the discharge is completed, the stop switch 606 is activated. Thus, the machine function is configured to be initialized.

  The operation of the garbage disposal device according to the present invention configured as described above will be described. When garbage is thrown into the reaction chamber 111 of the hopper 110 through the inlet 112 of the reaction tank 100, the temperature of the garbage in the reaction chamber 111 is raised to about 80 ° C. by the heating means 120 located at the bottom of the hopper 110. , The moisture contained in the food waste changes into steam, and at the same time, the stirring impeller 130 rotates in the forward direction and is uniformly dispersed and stirred by the stirring piece 132A of the stirring blade 132. In some cases, while colliding between the rotating stirring blade 132 and the crushing function unit 140, it is shredded to a size smaller than the appropriate size so that it can be quickly dried and decomposed.

  In addition, the steam generated from the garbage by the heater 122 in the heating means 120 in the reaction chamber 111 of the reaction tank 100 flows into the condenser 200 through the connecting pipe 240, and the steam that flows into the condenser 200 is , While the cooling fan 220 of the condenser 200 passes through the cooling pipe 220, its temperature drops rapidly and is condensed, so that it is separated into water and air, and the water flows into the automatic drain pipe 500 through the drain cock 212. The cold air is pumped to the deodorizer 300 by the blower 400 through the connecting pipe 360.

  Further, the condensed water supplied to the automatic drain pipe 500 through the drain cock 212 as described above is subjected to final filtration while passing through the fibrous activated carbon layer 520 and then discharged to the outside through the drain pipe 530, and is connected to the connecting pipe 360. The air sent to the deodorizer 300 by the blower 400 is reheated at a temperature of about 300 to 350 degrees by the electric heater 330 while passing through the heat supply pipe 310 of the deodorizer 300, and the catalyst of the deodorizer 300 After passing through the tube 320 and passing through the ceramic carrier 350 for preventing heat aging and a large number of platinum catalyst layers 340, the deodorized hot air is re-flowed into the reaction vessel 100 through the T-shaped connecting tube 370 to cause internal reaction. Helps increase the temperature in the chamber 111. On the opposite side of the T-shaped connecting pipe, when an internal air pressure load is generated in the reaction chamber 111, it is discharged to the outside through the cooling discharge pipe 380.

  On the other hand, when the above process is repeated continuously, the raw garbage initially put in the reaction tank 100 is completely dried and decomposed, so that only powder residue remains.

  Thereafter, when the agitation impeller 130 rotated by the drive motor 150 is rotated in the reverse direction, the inclined piece 132B formed on the agitation blade 132 of the agitation impeller 130 positions the powdered garbage in the middle portion of the shaft shaft 131. By gathering at the discharge port 113, the processed powder form by-product can be discharged smoothly through the discharge port 113 of the reaction tank 100.

  As described above, according to the present embodiment, the vapor generated during the dry decomposition passes through the condenser, and only the pure substance is discharged to the outside, and the air is not discharged to the outside. The air circulation recycling system is adopted so that the air exhausted to the outside is eliminated, there is almost no heat loss, and no bad odor is generated. Heat energy is minimized by using a stepped electric heater system, and the treated material is not sanitized and hygienic, and is recycled as organic fertilizer, and is processed with low energy and efficient operation structure. Reduce operating costs by reducing time. In addition, since the safety device is attached to ensure safety and ease of use, noise and vibration are minimized, and the machine is small, all items such as minimizing the installation space can be satisfied.

  As mentioned above, although preferred embodiment of this invention was described referring an accompanying drawing, it cannot be overemphasized that this invention is not limited to the example which concerns. It will be apparent to those skilled in the art that various changes and modifications can be made within the scope of the claims, and these are naturally within the technical scope of the present invention. Understood.

  The present invention crushes and squeezes garbage, forcibly dewaters it, disperses it with a stirrer and dries it, breaks it down with a crushing function part, breaks it down, passes the steam through a condenser, In this method, only pure substances are discharged, and air is recirculated into the reaction tank, and the air circulation inflow method is adopted to eliminate the air to be discharged to the outside. It is applicable to a new and improved garbage disposal device that can effectively achieve the treatment time and weight reduction effect without the pollution of sewage by forced dehydration and air pollution by heat incineration.

1 is an overall configuration diagram illustrating a garbage disposal device according to an embodiment of the present invention. It is a sectional side view of the reaction tank which is the principal part of the garbage processing device by the same embodiment. It is the perspective view which showed the stirring impeller which is the principal part of the garbage processing device by the same embodiment. It is the block diagram which showed the electric control part of the garbage processing device by the embodiment.

Explanation of symbols

DESCRIPTION OF SYMBOLS 100 Reaction tank 110 Hopper 111 Reaction chamber 112 Input port 113 Outlet port 120 Heating means 121 Heating frame 121A Heating chamber 122 Heating heater 123 Heat medium oil 130 Stirring impeller 131 Shaft shaft 132 Stirring blade 132A Stirring piece 132B Inclined piece 133 Rotating arm 140 Crushing function unit 150 Drive motor 151 Drive shaft 152 Soup racket 153 Chain 154 Chain adjustment gear 160 Temperature sensor 170 Heat medium auxiliary tank 200 Condenser 210 Support frame 211 Center hole 212 Drain cock 220 Cooling pipe 221 Cooling blade 230 Cooling fan 240 Connecting pipe 300 Deodorizer 310 Heat supply pipe 311 Guide hole 320 Catalyst pipe 330 Electric heater 331 Radiating blade 340 Platinum catalyst layer 350 Ceramic carrier 360 Connecting pipe 370 Connecting pipe 380 Cooling discharge pipe 400 Blower 500 Moving drain pipe 510 Drain cylinder 520 Fibrous activated carbon layer 600 Electric control unit 601 Operation time operation panel 602 Fault lamp 603 Power switch 604 Operation switch 605 Discharge switch 606 Stop switch

Claims (11)

The top and side surfaces of the hopper having the reaction chamber sealed inside are formed so that the inlet for allowing the garbage to flow into the reaction chamber and the outlet for discharging the treated garbage from the reaction chamber are opened and closed by the lid. In addition, the lower part of the hopper is provided with heating means for heating the raw garbage put into the reaction chamber to generate water vapor, and the raw waste is stirred and dispersed in the reaction chamber of the hopper. The stirring impeller that is collected in the reaction chamber is installed so as to be rotated by a driving motor, and a crushing function unit is formed on the inner side surface of the reaction chamber so that the garbage stirred by the stirring blade is crushed. A tank;
A cooling pipe is connected between a plurality of support frames having an inner hole portion therein so as to communicate with the inner hole portion, and a cooling fan for blowing cold air is installed in a portion adjacent to the cooling pipe, Drain cocks are respectively formed in the lower stage portions of the both side support frames, and the one side support frame is connected so as to communicate with a hopper of the reaction tank through a connecting pipe so that the garbage is heated in the reaction tank. A condenser in which vapor generated while passing through the connecting pipe through the support frame and the cooling pipe is condensed by contact with cold air and separated into water and air;
A heat supply pipe having a guide hole therein and a catalyst pipe are formed so as to communicate with each other, an electric heater is fixedly disposed inside the heat supply pipe, and a ceramic for preventing heat aging is provided inside the catalyst pipe. A support and a large number of platinum catalyst layers are fixedly arranged at appropriate intervals, the heat supply pipe is connected so as to communicate with the other support frame of the condenser through a connection pipe, and the catalyst pipe is connected to a hopper of the reaction tank. The cooling pipe was connected so that the catalyst pipe and the hopper of the reaction tank were connected so that the catalyst pipe and the hopper of the reaction tank were connected, and passed through the condenser. The air is deodorized while passing through the heat supply pipe and the catalyst pipe, and hot air that has passed through the heat supply pipe and the catalyst pipe is re-flowed into the reaction tank through the connection pipe and simultaneously raises the temperature in the reaction chamber. The reaction h A deodorizer which air micro discharged to the outside through the cooling discharge pipe and the air pressure load is generated in the members;
A blower installed on a connecting pipe connecting the condenser and the deodorizer, and pumping the air passing through the condenser to the deodorizer;
A number of fibrous activated carbon layers are stacked inside an automatic drain pipe connected to communicate with a drain cock formed at a lower part of the support frame of the condenser, and a drain pipe is disposed below the drain cylinder. A garbage disposal device formed so as to communicate with the automatic drain pipe so that the condensed water generated in the condenser passes through the fibrous activated carbon layer and is finally filtered and discharged. .   A temperature sensor is installed in the hopper of the reaction tank, and the heater is configured to be controlled by a controller in accordance with a signal from the temperature sensor. When a tank is installed and the heat transfer medium oil in the heating means undergoes thermal expansion by the heater, it goes up to the heat transfer medium auxiliary tank. The garbage disposal device according to claim 1, wherein the garbage disposal device is configured to escape to the outside.   In the heating means, a heating frame having a heating chamber therein is integrally coupled so as to partially wrap the lower and side surfaces of the hopper, and a heating heater that is operated by electricity is disposed horizontally in the heating chamber. The heat medium oil is stored in the heating chamber, and the hopper is indirectly heated while the heat medium oil is heated by the heater. The garbage processing device according to claim 1.   The agitation impeller of the reaction vessel is disposed horizontally in the reaction chamber of the hopper so as to be rotatable about a shaft axis, and a number of agitation blades are fixedly coupled radially to the shaft axis by a rotating arm on the shaft axis. The garbage processing device according to claim 1, wherein the garbage disposal device is provided.   A large number of cooling blades are formed at the end of each cooling pipe of the condenser, and the heat transfer effect is increased by a cooling fan by widening the contact area with the outside, and the water vapor passing through the cooling pipe is increased. Condensation is formed more efficiently, and the electric heater of the deodorizer is formed with a plurality of radiating blades, and the temperature of the internal air entering the blower is increased by increasing the contact area with the outside. The garbage disposal apparatus according to claim 1, wherein the garbage is raised by an electric heater and is moved to the catalyst pipe while maintaining the inside of the heat supply pipe at an appropriate temperature.   In order to extend the life of the platinum catalyst layer, the catalyst tube of the deodorizer uses a ceramic carrier for preventing heat aging as a pretreatment agent. Many platinum catalyst layers take into consideration the contact area, the air volume and the air speed of the blower, etc. 3. A garbage disposal apparatus according to claim 1, wherein a platinum catalyst layer having a three-stage multilayer structure is constructed.   The power consumption capacity supplied to the heater of the heating means adopts an electric supply system in stages, and by initially supplying the maximum installation force, the heat transfer medium oil is heated at an early stage and the reaction is performed. The temperature in the chamber is quickly raised so that the power consumption capacity supplied to the heater is supplied at about half of the initial installed power, and the temperature in the reaction chamber is about the set temperature. It is heated until it is transmitted to 80 ° C., and after that, when the temperature in the reaction chamber reaches about 80 ° C., the power consumption capacity supplied to the heating medium oil heater is supplied at about 1/4 of the initial installed strength. Thus, by allowing the operating temperature in the reaction chamber to be continuously maintained at about 80 ° C., the electric energy supplied to the heater until the end of the work is minimized. Only in and driving, garbage processor according to claim 7, characterized in that it is configured to save power consumption.   A soup racket is fixedly coupled to each of the shaft shaft and the driving shaft of the driving motor, and the soup racket is coupled so as to be interlocked with a chain. The drive motor that rotates the stirring impeller is configured to maintain the tension, and a low-speed geared motor (Gear Motor) that can rotate in the forward and reverse directions is applied. The garbage disposal device according to claim 4, wherein the garbage disposal device is configured to be capable of rotating about four times per contact.   The plurality of stirring blades are configured such that the stirring pieces for pushing and stirring the garbage and the inclined pieces are inclined at a fixed angle on the back surface, and the inclined pieces are symmetrical about the intermediate portion of the shaft shaft. When the shaft rotates in the forward direction, the garbage is uniformly dispersed and stirred at both ends of the shaft shaft while being pushed by the stirring pieces of the stirring blade. When the shaft rotates in the opposite direction, the garbage is The garbage is collected so as to be collected at an intermediate portion of the shaft shaft while being pushed by the inclined piece of the stirring blade, and the processed material can be automatically discharged. Processor.   The crushing function unit fixedly coupled to the stirring impeller of the stirring impeller and the inner wall of the reaction chamber of the hopper is installed adjacent to each other, and the garbage is cut and crushed between the rotating stirring blade and the crushing function unit. The garbage disposal device according to claim 4, wherein the garbage disposal device is configured as described above.   The electric control unit has an operation time operation panel and a failure lamp that notifies failure and machine stoppage when overheated and overloaded. The power switch is a switch that accepts primary incoming electricity, and the operation is completed when the operation switch is pressed. All functions are automatically performed, and when the discharge switch is pressed, the final by-product is discharged to the outside. When the discharge is completed, the stop switch is pressed to initialize the machine function. The garbage processing device of Claim 2.

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